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HomeMy WebLinkAboutCT 82-12; Carlsbad Highlands; Hydrology Study; 1986-10-16” " L n- - N h m n n- - "C do c NI?O 6-Hour Precipitation (inches)? OVIOVIOLD 0FJm 0 m ." "_ ~ 0 rD an * m (u: c ua 0 .Q 0 0 m N 0 u, c c 0 '. L/L a RASN A J i .'.- if 3/32, Oescriplion AreaCA,! 2.6 I3 Ac. Refaewe WtFFICIENT OF RUNOFT: G (conrider probable development) pveloped Areas (Urban) soefficient " C *' % Land Use Residential: Slngle famlly I fi Multi-Unlts hqobile Homes Rml (lots greater Commercial (2) 80% Impervious . " Industrial (2) 90% Impervious than Vi! acre) DME Or CONCCNTRATIONTC (Chafl 8-11 Hl .R. H. - A k - C -40 .45 .so .45 .50 .60 .45 .so .ss .SO .35 .40 .70 -75 -80 *eo . e5 * 90 .ss = .65 = .45 = .85 = .95 = c = I0.R. L. L= Distance in Mllcs H- Helpht ln hct ,;- PV DATE .- SHEET NO. OF - ctiECKED DATE JOB JOB NO. YZ 7t Description AteaCA) 2.747 Ac. FOEFrICILNT OF RUNOrF: C (conrider probnble development) pevelo~cd Areas (Urban) n Land Use ResldentFsl: Single Family loa Multi-Units Mobile Homes Rwzl (lots greater than 1/2 acre) Commercia1 (2) I - 80% Impervious Industrial (2) 90% Impervious H1.R. H. L0.R. L. Epcfficient " C '* 6011 Type ( 1 ) A - €! - C 2 -40 -45 .so .s5 - .45 .so .60 @ . .45 .so .55 .65 = .30 .35 .40 -45 = .70 -75 EO .85 = .80 .85 .90 .95 = L= Distance in Miles H- Height In Feet z 6f 7 3 of . , a ,- 1 WETFICILNT OF RUNOFF: C (conrIder probable development) pevelomd Areas (Urban] % Und Use Residential: Single Family .40 .45 -50 .fS - IVO 7) Multi-Unitr .IS .so .60 @= h3obile Homes .45 .50 .55 .6S = Rml (lots greater than 1/2 acre) .30 .35 .4@ .45 = Commercia! (2) - 8@% Impemlous Industrial (2) 90% Impemlous H1.Pt. H. L0.R. 1. .70 .75 . eo .85 = - .eo .85 .90 .95 = L= Dlstance In Miles H= Height In Feet COtrFlClENT OF RUNOFF: C (conolder probable development) peveloptd Areas (Urban) Y land Use Resldential: Single Family hqobile Homes Rml (lots greater than 1/2 &me) Commercia! (2) - 8@% Ir;,pewfous f- Industrial (2) 9@% Impewlous Hi .R. H. b.R. L. soefficient " C * 6011 Type ( 1) - A B - C B .40 .4s * 50 .5s - .45 .so .60 Cjc& .45 .50 .ss -65 = .30 * 35 .4@ .45 = .70 -75 * eo .85 = .eo .85 .96 .95 = L= Distance in Mller H= Height In reet HY DROLOCY CALCULATIONS - aarwvm METHOD - B\' ChcCKED DATE JOB JOB NO. (- DATE SHEET NQ. OF - s rqo Description AreaCA,! ~.QS Ac. 8a 6 i*I Reference Reridentisl: A B E 02, - Slngle F'amlly .40 -45 -50 .55 - - I @ Multi-Unlts .45 .so .60 &= - Nobile Homes .45 .SO -55 .65 = - Rw~l (lots greater than 1/2 acre) .30 -35 .4c .45 = - Commercia! (2) .70 .75 .eo .e5 = - i- 80% Impervlous Industrial (2) 90% lmpewlous H1 .R. H. b.R. I. .BO .85 .90 .os = - HY DROLOCY CuCULATlONS - RRTIHAL MCWOO- SHEET NQ. OF - ChLCKED DATE JOB JOB NO. GOEFFICIENT Or RUNOFf: C (conelder probable development) pevelo~ed Area6 (Urbsn) x land Use Resldential: Slngle Famlly jh3 Multi-Unltr hqoblle Homes Rml (Jots greater than 1/2 Bcre) Commercia1 (2) 80% Impervlous I- Industrial (2) 90% Impervlous H1 .R. H. b.R. L. 6011 Type ( 1) affictent C " .30 .70 .eo .35 .4c .75 .OO .85 -90 L= Distance In Miles H= Helght In reet HY DROLOCY CALCULATIONS - RAT&W4L MLTHOO- SHEET NQ. OF - ChcCKED DATE JOB JOB NO. FOtFS7CIrNT Or RUNOrT: C (conrlder pmbeb1e development) PveloFed Areas Nrbsn) x land Use Resldentbl: Slngle Family /@ N;ultl-Unlts Mobile Homes Run1 (lot5 greater than 1/2 acre) Commercia1 (2) - I 80% Impervious Industriel (2) 90% Impervlous H1.R. H. b.R. L. Coefficient C " 6011 Type ( 1) A! B - =@ -40 .4s .so .5s - - .45 .so -5s .65 = - -30 .35 .4c .45 = - -70 -75 . eo .85 = - .eo .85 .so .os f - WWFICIENT OF RUNOFT: C (conrider probable development) peveloped Areas (Urkmn) x Und Use Residential: A B E Slnglc Famlly -40 -4s .50 / UI Multi-Unltr .4s .so .60 hfobile Homes .45 .so .Sf -.- Rml (lots greater than 1/2 acre) -30 .35 .40 Commercial (2) f. " 80% Impervlout Industrial (2) 90% Impervious (Cha17 B-1) H1.R. H. .70 -75 * eo .eo .e5 .90 B .55 - - a- .95 f - LA3.R. L. L= Distance in Mllcs H= Hclght In hrt t I L I I I I i I I 1 I I I 4 pvelopcd Areas (Urban) x Land Use Rerldenthl: A B - C Single Family -40 .4s .so .s5 - I! Multi-Units h3obile Homes Run1 (lots greater than 1/2 acre) Commercia! (2) 8D% Impervious i- f Ul) Industrial (2) ', 90% Impewious Hl .R. H. L3.R. L" .45 .so .60 .7G = - .45 .so .55 .65 = .30 .35 .40 -45 = - .70 -75 .80 .85 = - L= Dlrtance ln Mllcr H= Hclght In Feet ~EFTICIENT OF RUNOTT: C (consider probable development) peveloDed Ares6 (Urban) x Land Use Residential: Slngle Famlly Multi-Units h4oblle Homes Rml (lots greater than 1/2 acre) Commercia! (2) t- 80% Impervlous 1 LA Industrlsl (2) 90% Impervious , H1.R. H. LA3.R. L. fficlent * C " Soil Typc 1 ) h B - C B -40 .IS .so .5s - - .45 .so .60 .7G = .45 .50 .5s .65 = - .30 .35 .4D .45 = .70 .75 -80 .e5 = L= Dlstanoe ln Miles H= Height In Feet ChcCKED DATE JOB JOB NO. Residcntisl: A B - C E - Slngle Famlly Multi-Units Mobile Homes RWEI (lots greater than 1/2 acre) .30 .35 .40 .45 = - Commercia! (2) 1.- 80% Irrlpervlous Industrial (2) 90% Impervious .70 .75 . eo .e5 = - .eo .E5 * 90 .?5 = - L= Dlctance ln Miles H= Hclght in tttt CHtCKED DATE JOB JOB NO. 7pI Description - AteaCA) d,JAb Ac- WtrFlCIrNT OF RUNOrT: C konrldcr probable development) peveloped Areas (Urbnn) x Land Ute Residential: h B - C E Single Family -40 .4s -50 .s5 * Multi-Units .45 .50 .60 .&a hfobile Homes .4s .50 -55 -65 = Rw~l (lots greater than 1/2 acre) .30 * 35 .40 .4s f - Dh!E Or COh’CChlF&TIONTC (Chafi 8-11 H1.R. H. b.R. L. .70 .75 . eo .BS = - .eo .e5 -90 .9s = - c =& HY DROLOCY CALCULATIONS - RATIOU~L METNOD- SHEET NQ. OF - CHtc-KED DATE JOB JOB NO. Description AreaCA,! 0.f53 Ac. lY37 Referonce WtWICIENT Or RUNOrT: G Cconmlder probable development) pveloprd Areas (Urban] % Land Use J;gtfficitnt " C " 6011 Type ( 1) RerldentIal: A k - C P - Sing le Pam lly Multl-Units hfobile Homes .4D .4s .so .ss - - .IS .so .60 a .45 .50 -55 .65 = R-1 (lots greater than 1/2 ncre) .30 .35 .4@ .45 = - Commercia! (2) r 80% Impervious Industriel (2) 90% Impervious HI.&. H. l0.R. L. .70 .75 -80 .E5 = .BO .85 .so .95 = L= Distance ln Mller R- Height In rcet pevelo~ed Areas Nrban) x Land Ute Rerldential: Coeffieicnr " C " So11 Typc 1) €! B - C E Slngle Family -40 .45 -50 .s5 = Multi-Unlts hqobfle Homes /m Rml (lots greater than 1/2 acre) Commercial (2) f' ~ .- 80% Impervlour Industrial (2) 90% Impewlous 1 -4s .so .60 .7G = .45 .so .55 .65 = .30 .35 .40 , .4h= 6. 7, .70 .75 . eo .85 = .BO .85 .90 .95 = - L- Dlrunce ln Mllcr H- Height In Feet FOtrrlClrNT OF RUNOFF: Q (conrider probable development) mveloved Areas (Urban) 96 Land Use Residential: Single Family Multi-Units h4obile Homes ~g.Vt! R~I (lots greater than I/Z acre) Commercial (2) t" 80% Ir~~pervlous 4/,7"Industrial (2) 90% Impervlous nME Or CONCfNTPATIONTC (CbR B-1) H1 .R. H. b.R. L. A - k - C -40 -4s -50 .I5 .SO .60 .45 .so .ss .30 .35 -40 .70 .75 . BO .BO .B5 .90 L= Dtstance ln Wtles H= Hclght In Feet x land Use Rerldentinl: A k Slngle Famlly -40 .45 IN ~u~ti-~nits .45 .so hqobfle Homes .45 .so Rum1 (lots greater than 1/2 acre) .30 .35 Commercia! (2) .70 -75 (" 813% Impervious "_c Industrial (2) .eo . e5 90% Impewlous ! E .so .60 .55 .40 * 80 .90 (Cbn B-1) H1.R. H. U.R. L. .55 - - .95 = - ~OtrFICIENT Or RUHOFr: C (conolder probable development) pvelo~cd Areas (Urban) x land Ute Resldential: A E - C B Single Famlly .40 .45 -50 .55 = - ! d Multl-Unfts .IS .so .60 @- Mobile Homes .45 .so -5s .65 = - Rwz.1 (lots greater than 1/2 ecre) .30 -35 .4@ .45 = - .70 .75 . eo .85 = - .eo . e5 -90 .95 = - L= Distance in Wlks H= Height In Feet Form by; A.M. 7, i 'I .* i XEi ". " , , .. a Mr 1- ,- \ CtltCKED DATE JOB JOB NO. De scr ipl ion &ea CA) 2 353 bc. Bo 5 ifi Refironce fi Multi-Unltr h5obile Homes RUE] (lots greater than 1/2 acre) Commercia! (2) r 80% Impervious Industrial (2) 90% Impervious (Cbn 8-1) H1.R. n. L0.R. L. .eo . E5 -96 .95 = - CktCKED Description Area CA (. DATE JOB 10B NO. Residentisl: A k - c Single Family .40 .45 .so Multi-Units .45 .so .60 hJoblle Homes .45 .so .55 !fl Rml (lots greater than 1/2 acre) .30 .35 .4c Commercia! (2) .70 .75 . eo 80% Impervious (r \ Industrial (2) 909. Inpewlous Hi .R. H. 1P.R. L. .eo .85 -90 L= Dirt~nce in Miles H= Height in reel .95 = - Ref Bb” ChtCKED DATE JOB JOB NO. t UATL‘ bldVb SHEET NQ. OF - Rerldential: Slngle Famlly Multi-Unltc htoblle Homes R-1 (lots greater than 1/2 acre) C:ommercia1 (2) t“ 80% Impewlous Industrial (2) 90% Impewlous HI .R. H. L0.R. L. B -45 .5s = - .IS .so .60 .I5 .so -5s .65 = - .30 .3s .4c .45 = - .70 .75 . BO .85 = - .BO .85 -96 .95 = - DATt A=, SHEET NQ. OF - ChtCKED DATE JOB JOB NO. FOtrFICIrNT OF RUNOFF: C (conolder probnble development) pvelowd Areas (Urban) 16 Lsnd Use Residential: A B - C E Single Famlly -40 .IS .so .55 = - Multi-Units .IS .so -60 @= Mobile Homes .45 .50 .Sf .6S = - Rw~l (lots greater than 1/2 acre) .30 .35 .4c .45 = - - Commercial (2) - 80% Impervious Industriel (2) 90% Inpewlous n1.R. H. b.R. 1. .70 .75 . EO .85 = - -80 . a5 .90 .05 = - pOtFFlCIrNT OF RUNOFF: C (conolder probable development) pvelomd Areas (Urban) x Land Use Residential: Single Famlly A B - C 6J .40 .45 .SO' .55 - - Multi-Unlts .4s .so .60 &= a hlobile Homes .45 .50 -55 .65 = - Rursl (lots greater than 1/2 acre) .30 .35 .4c .45 = " Commercia! (2) .70 .75 .eo .85 = - c- 80% Impervious Industricl (2) 90% Impervious W1.R. H. b.R. L. .eo .85 .96 .:5 = - pOrFrICIrNT OF RUNOFF: G (conolder probable development) pevelopcd Areas Nrban) x Land Use Residential: A k - C E Slngle Famlly -40 .4s .so .ss - - hlobile Homes .4s .so .60 - .45 .so -55 .65 = - Rrsl (lots greater than 1/2 acre) .30 .35 .4c -45 = - Cornmerc$a! (2) - 80% Impervious Industrial (2) 90% Impervlous H1.R. H. b.R. L. - -. .70 .75 -80 .e5 = - .ED . E5 .90 .os = - L= Distance ln Miles H= Height In rcet JOB NO. CH~CKED DATE JOB Dcscriplion AeaCA) /,OOf Ac. 80 5 til /I 70 $QtFFlCIrNT OF RUNOFT: C (conrlder probable development) Developed Areas (Urbon) x Land Use Resldenthl: A B - C E Single Famlly Multi-Unlts -40 .45 .so hJobile Homes .45 .so .ss .6S = - RUR~ (lots greater than 1/2 acre) .30 .35 .4c .45 = - Commercial (2) .70 .75 . eo .E5 = - c_ 80% Impewlous Industrial (2) 909. Inpewlous .eo .85 * 96 .os = - t= Dlrtanoe ln Mlles H= Hclght In feel Soil Type ( 1) welent " C " Reridentlsl: A B - Slngle Famlly -40 .45 -50 -55 - - "6 Multi-Unlts hqoblle Homes .45 .45 .so .55 .65 = Rml (lots greater than 1/2 acre) .30 .35 .4c .45 = - Commercial (2) i c 80% Ir;.pervlous Industrial (2) 90% Impervious .70 .75 -80 .8S = - .BO .E5 .90 .95 = - L= Distance ln Miles H= Height In Feet ~OtrrICItNT OF RUNOFF: C (conrlder probable development) pveloped Ares6 (Urban) Coefficient " C " 6011 Type ( 1) % Land Ute Rerldenthl: A k Single Famlly .IO .45 /fi ~ult~-~njtr .45 .so Mobile Homes .45 .50 Rursl (lots greater than 1/2 acre) .30 .35 Commercial (2) .70 .75 - 80% Imperwlous Industrial (2) .80 .85 90% Impervious E -50 .60 -55 .4c -80 -90 Hi .R. H. X0.R. L. B .55 - - .05 = - CHtCKED DATE JOB JOB NO. WrrtICIfNT Or RUNOrT: C (conrlder probable development) ~veloped Areas Niban) % Land Use Resldenthl: A B - C Slngle hmily .40 .4s .so .s5 - - /I$ Multi-Unltr .45 .so .60 &= & htobile Homes .45 .50 .55 .65 = - Rml (lots greater than 1/2 acre) .30 -35 .4c .45 = " 6) Commercia! (2) - 80% 1rr.penrlous Industrial (2) 9@% Impewlous H1.R. m. .70 .75 . SO .e5 = - .ED .85 .90 .95 = - t,.R. L. L= Dlrmnce in Mlles H= Height in Feet CHtCKED DATE JOB JOB NO. Description A~~CA~ 2.625' ac. 31 33 WtrrlCIENT Or RUNOTT: C (conrlder probnble developmen0 pevelopcd Area6 (Urban) x Land Use GoefficlenT C I Soil Type ( 1 ) Resident&]: Slngle Famlly Multi-Unlts Mobile Homes A B - C .40 .4s . SD .s5 - - .45 .so .60 8- .4s .50 .5s .65 = - Rursl (lots greater than 1/2 acre) .30 -35 .4c .45 = - .70 . 75 .80 .e5 = - ( Industrial (2) -80 .85 -90 .os = - 909. Impervlous W1.R. H. L0.R. L. t= Distance in Miles H= Hclght In Feet WtFFICKNT OF RUNOFF: E (conrider probable development) Jkvclo~cd Areas (Urban) Y tand Use Residential: A B - C P - Single Family .40 .45 * so .5s - - Multl-Unlts .IS .so .60 - hfoblle Homes .45 .50 -55 -65 = - RD~ (lots greater than 1/2 acre) .30 -35 -40 .45 = - Commercia! (2) - 80% Irr'pervlous Industriel (2) 90% Inpewlous nh!E Or COh'CfhTRkTIOh'TC (Chi? 8-11 H1 .R. W. b.R. L. -70 .80 .85 .so .95 = - L= Distance in Miles H= Height ln Feet GOEFFICIENT OF RUNOFF: C (conmlder probable development) pveloped Areas (Urban] 96 Land Use Resldentlal: Ib 'Single Famlly Multi-Unlts Moblle Homes 6011 Type ( 1 ) Goefficient " C " .45 .sa -5s -65 = Run1 (lots greater than 1/2 acre) .30 -35 .40 .45 = Commercia! (2) 80% Impervious (- Industrial (2) 90% Impervlous H1 .R. H. b.R. L. .70 .75 .80 .e5 = .BO .85 .so .95 = L= Distance ln Mller H= Height in rett ~OtFFlClENT OF RUNOTr: (conrider probable development) peveloped Aress (Urban) x Land Use Resldential: - A B - c @ I@ Single Famlly .40 .45 -50 & .J7- Multi-Unlts .4s .so .60 .7G = hqoblle Homes .45 .so .55 .65 = Rml (lots greater than 1/2 acre) .30 .35 .40 .45 = Commercia! (21 80% In~pewlouS . -. Industrial (2) 90% Impewlous .70 .75 . BO .85 = .80 .85 .90 .95 = L= Distance in Miles H= Hclght tn rest peveloDcd Areas (Urban] )b Land Use Reridentlal: - A k C SIngle Family .40 .45 .so .55 - Multi-Units .4s .so .60 .7G = Mobile Homes .45 .50 -55 .65 = nt37 ~urrl (lots greater than I/Z acre) .30 .35 .40 .45 = ,‘2ZLbt - E _c Commercial (2) 80% Impervious ( Industrial (2) 90% ImpewIous .70 .75 . eo .e5 = .eo .85 * 90 .g5 c .47/V! b.R. 1. L= Distance ln Miles H= Height in Feet 1 .manlTOU onglnoor1ng company HY DROLOCY CALCULATIONS - anrtmRL METHOD- SHEET NO, OF - FOErrICIENT OF RVNOTr: C (conrtder probable development) peveloped Ares6 (Urbsn] % Land Use Residential: f@ Slngle Famlly Multi-UnIts .45 .50 .6D .7G = hqoblle Homes .45 .so .55 .65 = Run1 (lots greater than 1/2 acre) .30 .35 .4D -45 = Commercial (2) 80% Ir;,pervlous c- Industrial (2) 90% Impervious fJME Or CONCChTRATIONTC (Chstt 8-1) n1.h. H. U.R. L. .70 .75 .eo .85 = .eo .85 -96 .95 = ~otrrlClENT OF RUNOFr: C (conmider probable development) peveloped Areas (Urban) x Land Use Residential: - A B - c Slngle Famlly -40 .45 * 50 (fl Multi-Unfts .4s * 50 .60 Moblle Homes .45 -50 .55 Run1 (lots greater than 1/2 acre) .30 -35 .40 Commercia! (2) 80% hpervlous (r Industrial (2) 90% Impenrious .70 .75 . BO .BO .85 .90 L= Distance in Miles H= Height in Feet .55 - .65 = -45 = .85 = .95 f c ..&KED DATE JOB JOB NO. P Description AreaCA) O. 7C8 Ac. 8a 5 in Refetcnce FOtFFlCIENT OF RUNOFF: G (conrider probable development) pevelowd Areas (Urban) x Und Use Residential: SIngle Famlly .40 .IS .so .55 = A&" ulti-Units .IS .50 .60 hqoblle Homes .45 .so .ss .65 = Rml (lots greater than 1/2 acre) .30 .35 .40 -45 = Commercia1 (2) 80% Impervious e- Industrial (2) 90% Impervious H1.h. H. L3.R. I. - -. .70 .75 .80 .85 = .80 .85 -90 .95 = peveloped Areas (Urban) % Lsnd Use Rerldential: SIngle Famlly IJO ~u~tl-~nitc A k - C .40 .45 .30 .55 - .IS .so .60 &L .id hfobile Homes .45 .so .55 .65 = Run1 (lots greater than 1/2 acre) .30 .3s .ID .45 = Commercia1 (2) E@% ImpentIous ( ,- Industrial (2) 90% Impewlous .70 -75 .eo .85 = .80 .85 .90 .95 f ~OEFrlCIENT OF RUNOrT: C (conrider probble development) pveloped Areas (Urban) x Land Use Residential: - A B - C Slngle Famlly -40 .45 .so .s5 - /IO Multi-Units .4s .so .60 @= 6.W h¶oblle Homes .45 .50 .Sf -65 = RWXI (lots greater than 1/2 scre) .30 * 35 .40 .4s = Commercial (2) 8@% Impervious ,- Industrial (2) 90% lmpentlous .70 ,75 -80 .85 = .80 .85 * 90 .95 = pevelo~ed Areas (Urban) % Land Use Resfdentis]: Single famlly I VD Multi-Untts Mobile Homes Soil Type ( 1 ) Coefficient *' C " - A k - C @ .40 .45 -50 .55 - .IS .50 .60 @ ,7d .45 .so .55 .65 = Rwl (lots greater than 1/2 Bcre) .30 -35 -40 -45 f Commercial (2) - 80% Impervious I Industrial (2) 90% Impervious .70 .75 . eo -85 = .eo I85 .90 .9s = L= Distance in Miles H= Height in Feet FOtFrlCTENT OF RUNOFF: C (conrider probable development) peveloped Areas (Urban) x Lsnd Use -40 .45 .so .s5 - .45 .so .60 @ Mobile Homes .45 .so .55 -65 = RWI (Jots greater than 1/2 sere) .30 .35 .4D .45 = Commercia! (2) 80% Impervious f- Industrial (2) 90% Impewlous M€ Or CONCEhTP.kTIOh'TC (Chan B-1) H1.R. H. L3.R. L. .70 .75 .00 .85 = .BO -85 -96 -95 = L= Distance ln Miles H= Hrlght In Feet PveloDed Areas (Urben) 96 Land Use Resldentisl: Single Family I YU Multi-units h9obile Homes Run1 (Jots greater than 1/2 acre) Commercial (2) ," 80% Impervious t Industrial (2) 90% Impervious \ Hi .PI. si. b.R. L. Goelfielent '' C 'I Soil Type ( 1) - A B - C .40 .45 .so -45 .so .60 .45 .so .5s .30 .35 .40 .70 -75 .eo .eo .85 .90 .95 = - ptFFICIrNT OF RUNOFF: C (eonolder probable development) pveloped Are86 (Urban) Y Land Use 6011 Type ( 1) Epefficfent ** C Rerldential: h €! - C b Single Family -40 -45 .so ' .55 - Multi-Units .45 .50 .60 .70 = Mobile Homes .45 .50 .55 bl.oV Run1 (lots greater than 1/2 acre) .30 .35 .40 Commercial (2) 80% Impervious 6" .70 -75 -80 ' Industrial (2) .80 .85 -90 .95 = ,3103 90% Impervious - H1.R. - -. H. L0.R. L. L= Dlrtance ln Mlles H= Helght in Feet peveloDed Areas (Urban) x Land Use Eplfficlent C .1 6011 Type ( 1 ) Residential: l! B E B Single Famlly Multi-Units Mobile Homes -40 .45 . so .s5 = .45 .so .60 .7G = .45 .so .Sf .6S = f2,3< Rwzl (lots greater than 1/2 acre) .30 .35 .40 @=.2 3J 7 Commercia! (2) 80% Impervious (- I I.L> Industrial (2) 90% Impervlous (ChaR 8-1) H1.R. H. L6.R. L. .70 .75 . eo .e5 = -80 .85 .so L+ Dlrmnce ln Mlles H= Height In Feet ?)I DATL SHEET NO, OF - ! i. AKED DATE JOB JOB NO. 78/ FOEWICIENT OF RUNOTr: C (conrider probable development) &kvelopcd Area6 (Urban) x Iand Use ResIdentLsl: SIngle Famlly Multi-Unltr hfoblle Homes Rurel (lots greater than 1/2 acre) Commercial (2) r 80% Impervious Industrial (2) 90% Impervlous H1.R. - -. H. b.R. L" .4s .50 .60 .7G = .45 .50 .Sf .65 = .30 -3s .40 -45 = .70 .75 . eo -85 = -80 .85 .90 .95 = L= Dlrtance in Miles H= Height in Fret ~OtFFlCILNT OF RUNOFF: C (conmlder probable development) mveloped Areas (Urban) x Land Use Rerldcntial: 1 b0 Slngle Famlly Multl-Unlts Moblle Homes Run1 (lots greater than l/Z acre) Commercia! (2) 80% Impervious - Industrial (2) 90% Impewious A B - c .40 .4s .so .45 .so .60 .45 .so .ss .30 -35 .40 .70 .75 .BO .80 .85 .90 L= Distance in Miles H= Height in reet @ .a- .7G = -65 = -45 = -85 = .95 = ~OtFFICILNT OF RUNOFT: C (conrlder probable development) Jkveloved Areas (Urban] % Land Use F=ff 6011 Type ( 1 ) iclent *' C Resldentlsl: A B In Slnglc Family .40 .IS Multi-Unfts .IS .so h3oblle Homes .45 .so Rum1 (lots greater than 1/2 acre) .30 -35 Commercia! (2) .70 .75 (" 80% Impervious Industrial (2) .so -85 90% Irnpervlous .60 .7G = .55 .65 = .4D .45 = * so .e5 = * 90 .95 = TIME Or COh'CChTRAfIONTC (Chalt 8-1) H1 .R. H. X0.R. X.. L= Dlrmnce ln Milts H= Height In Fret b -40 -45 .IS .so .70 . .eo . ¶S .4D .4f = - -75 -6D .e5 = -85 .OD .s5 - .30 .3s .IO -70 .IS -60 -60 .85 .OD Resldenthl: A B E E Slngle Family Multi-Units -40 .45 .so .s5 - - .IS .so .60 .7G = - Mobile Homes .45 .50 .55 .65 = - RWCI (lots greater than 1/2 acre) .3G .35 .4c .45 = .17/0 Commercia! (2) 80% Irr,pervlour r bv Industrial (2) 90% ImpewIous .70 .75 -80 .e5 = - .80 .85 .90 .05 = & L0.R. L. L= Dlrtancc in Miles H= Height In Feet RY DATE SHEET NQ. I ,- OF - c..e;CKED DATE JOB JOB NO. peveloped Area6 (Urban) x Land Use Residential: Single Family Multi-Unlts Mobile Homes sO.?f R-1 (lots greater than 1/2 acre) Commercial (2) 80% Impervious (- +f. zf Industrial (2) I 90% Impervious A E! - C -40 .4f .so .45 .50 .60 .45 .so -55 .30 -35 -40 .70 -75 -80 .eo .85 -90 1- Dlrance in Mller H= Hclght In Feet B .55 - - .g5 = y17( ~OrFrlClENT Or RUNOFS': G (conrider probble development) peveloved Areas (Urban) x Lsnd Use coefficient C 'I 6011 Type ( 1 ) Residential: A Single Famlly .4D .45 .so Wultl-Units .45 .SO .60 htobile Homes .45 .so .55 R-1 (lots greater than l/Z acre) .30 .35 .4@ B - C Commercia! (2) E@% Impewlous (- Industrial (2) 90% Impewlous (Chan 8-11 WJ .R. H. L0.R. L. .7@ -75 -80 . BD .85 .90 L= Distance ln Miles H= Height ln rcet e .55 = - WErrICTENT OF RUNOTr: C (conolder probable development) pevelo~cd Areas (Urban) % tand Use Residential: Slngle Family Multi-Units Mobile Homes t R~I (lots greater than I/Z acre) Commercial (2) i' 80% Irr,pervlous - Industrial (2) 90% Impervlous \ TIME OF CONCCNTRATIONTC (Cbn 8-11 Hl .R. H. I0.R. L. A - B E -40 .IS .so ' .I5 . sd .60 .45 .so .55 .30 .35 .4D .70 .75 .80 .eo .85 .90 L= Distance ln Miles H- Hclpht in Feet P .55 - .7G = .65 = @ = ,3190 c = 0,Sv I. (-- I' ." L" .r j” 6 bC b Residential: Slngle Family Multi-Units Mobile Homes //;O Rml (lots greater than 1/2 acre) Commercia1 (2) 80% Impervious (- Industriel (2) ' 90% Impervlout .IS .so .60 .7G = - .45 .50 -5s .65 = - .30 * 35 .40 -45 = 3 .70 -75 . BO -85 = - .ED .85 .90 .95 = - HY DROLOCY CwCULAnONS - aArt,wm METHOD - SHEET NQ. OF - DATE JOB JOB NO. ~LFrlCIENT Or RUNOTr: G (conolder probable development) pvelopcd Areas Nrbsn) x Land Vre Resldential: A k - C Single Family Multl-Unlts -40 .45 .so .5s f - .45 .so .60 .70 = - Mobile Homes .45 .50 -55 .65 = - Io Rw~l (lots greater than 1/2 acre) .30 .35 .4@ Commercia! (2) 80% Impervious - Industrial (2) 90% Impervious .70 .75 . eo .85 = - .eo .85 -96 .95 = - b.R. L. t= Distance in Mllcr H= Height In Feet Resldenthl: Slngle famlly G=ff Soil Type ( 1 ) icfent " C " .40 .45 .55 - - Multi-Unltr .45 .50 .60 .7G = - hfoblle Homes .45 .50 .55 .65 = - \ 11) Rml (lots greater than l/Z ecre) .30 .35 Commercia! (2) 80% IrrJpervious 6- - Industrial (2) 90% Impervious .70 .75 . eo .85 = - .eo .85 .90 .95 = - 1- Dlrtance In Mller H= Hclpht ln Feet HY DROLOCY CALCULATIONS - RATtWAL METMOD- SHEET NQ. OF - /I- C. KED DATE JOB JOB NO. WtFTlCIrNT OF RUNOrT: C (eonmider probable development) pevelo~ed Areas (Urban) n Land Ute Resldential: Single Family Multl-Units Mobile Homes / fl Run1 (lots greater than 1/2 acre) Commercia! (2) 80% Impervious - Industrial (2) 90% Impervlous H1.R. H. L.R. L. Eprfficient ., C n So11 Type ( 1 ) dl B -40 .IS -45 .so .45 .so .30 -35 .70 -75 .BO .B5 -50 .55 - - .60 .fG = - .55 .65 = - .4@ @> * eo .BS = - -90 .95 = - BY VATE SHEET NQ. OF - i. - KED DATE JOB JOB NO. Wvelo@ed Areas (Urban) x land Use Residential: Single Family c = ffl Soil Type ( 1 ) clent * C il E - C .40 .IS .so Multi-Units .45 .SO .60 hfobile Homes .45 .so .55 J 2kJ RWZI (101s greater than 1/2 ecre) .30 .35 .4@ Commercia! (2) 80% Impervious " - Industrial (2) 90% Impervlous H1.R. H. Ir0.h. L. .70 .75 .80 .BO .85 .90 L= Distance ln Miles H= Helght In Feet .55 - - .95 = * ". . DtFFlCTENT OF RUNOrF: C (conrider pkbnble development) peveloFed Areas (vrben) z land Vre Rerldential: Single Famlly Multi-Units h5oblle Homes 71.87 Rum1 (lots greater than 1/2 acre) Commercia! (2) 80% Imperwlous t- - Industrial (2) 90% Impervlous H1.R. H. L6.R. L. li B E .40 -45 -50 .45 .SO .6D .45 .50 -55 .30 .35 .40 .70 .75 . eo .80 .85 .90 L= Distance In Miles H= Hclght ln Feet d KED DATE JOB JOB NO. ~OtrrICIrNT OF RUNOFF: C (conrlder pmbable development) peveloped Ares6 (Urben) Y Lsnd Use Resldentlal: Single Famlly Multi-Units .45 .so .60 .fG = - h5obile Homes .45 .50 .Sf -65 = - zq,3 Rml (lots greater than 1/2 acre) .30 .35 .40 c4+ ./n9 90% Impewlous H1.R. H. b.R. 1. L= Dlrtancc In Miles H= Height in Feet HY DROLOCY CNCULATIONS - RATrCINAL METMOD - SHEET NQ. OF - C!” KED DATE JOB JOB NO. prWICIrNT OF RUNOTr: C (conrider probable dtvtlopment) pevelomd Art86 (Urbsn) x Land Use mfficltnt ** C ” 6011 Type ( 1 ) Rerldenthl: Single Famlly Multi-Units Mobile Homes h B E B .40 -45 .50 .55 - - .45 .so -60 .fO = - .45 .50 .s5 .65 = - .70 .75 .eo - 8 5 = .“” t Distance ln Miles U= Hclght In rret Rerldentisl: A B - C E Slnglc Famlly Multi-Units h4oblle Homes -40 .45 .so .ss = - .IS .so -60 .70 = - .4s .so .5s .6S = - .ZV Rurzl (lots greater than l/Z acre) .30 .35 .ID Commercia! (2) ED% Impervious 6- Iz/ - Industrial (2) 9D% Impervious .70 .75 * ea .E5 = - .80 .BS .90 -95 = 2 b.R. L. L= Dlrmnce ln Mllrr H= Hclght In Feet ~LrrICIrNT OF RUNOrTrs (conmlder probable development) pevelopcd Area6 (Urban! x Land Use Residential: - Single Famlly -40 .45 .so .55 = - Multi-Unlts -45 .5D .6D .fG = - hqoblle Homes .45 .5D * 55 .65 = - zlt Rwsl (lots greater than 1/2 acre) .30 .35 .4D Commercia! (2) 80% Impervious '- - Industrial (2) 90% Impervlour H1.R. H. U.R. L. .70 -75 . BO .85 = - .8D .85 .so @ .du'y HY DROLOCY CALCULATIONS - R4TIDURL METMOD- SHEET NQ. OF - C! - KED DATE JOB JOB NO. x Land Use Resldcnli~l: Single Famlly Multi-Units hqobile Homes ~Cl,t R~I (lots greater &an I/Z acre) Commercia! (2) 80% Impervious ‘r x Industrial (2) 90% Impervious \ H1.R. H” L0.R. t. h B .40 .45 -45 .so .45 .so .30 .35 .70 .75 .EO . E5 .SO .55 - - -90 .95 = & L= Distance ln Miles H= Helpht In Feet ~OLFTlCIrNT OF RUNOFF: C (consider probable development) pvelomd Areas (Urban) Y land Use Residential: A B E E - Single Famlly -40 .45 .50 .55 = - Multi-Units .45 .50 .60 .7cI = - hqobile Homes .45 .so * 55 .65 = - I VU Rurel (lots greater than 1/2 acre) .30 .35 -40 Cr".,': - I Commercia! (2) .70 .75 .80 .85 = - 80% Impervious I- - Industrial (2) 90% Impervious Hi .PI. €I. * 80 .85 -90 .95 = - ~~ fly SHEET NQ. (- OF - c XKED DATE JOB JOB NO. Description Area CA) &36 bc. 8a~~ Refemce prrrICIENT Or RUNOrT: C (conalder probable development) pveloped Areas (Urban) % Land Use Resldential: Soil Type ( 1) Coefficienr C " B Single Family -40 .4s -50 .ss - Mobile Homes .4s .45 .65 = RWEJ (lots greater than 1/2 acre) .30 .35 .40 .45 = Commercia! (2) 80% Irr,pewlous t- Industrial (2) 90% Impewlout Hi.&. - -. n. b.F-t. I. .70 .75 . so .E5 = .so -85 .90 .95 = HY DROLOCY CALCULATIONS - RATIONAL METHOD- SHEET NQ. OF - ChcCKED DATE JOB JOB NO. ~OErSIClENT Or RUNOFF: (conrider pmbnblc development) peveloccd Are06 (Urban) x land Use RerIdenthl: & k - C -40 .45 .50 .55 - - .45 .50 .60 h5obile Homes .IS .so .55 .65 = - RWZI (lots greater than 1/2 acre) .30 -35 .40 .45 = - HI .R. H. L2.R. L. .70 .75 .80 .85 = - .BO .85 -90 .95 = - B" DAlF e- SHEET NQ. I- OF - C..-iKED DATE JOB JOB NO. PLrrlCYrNT Or RUNOrT: C (conrider probnble development) pveloped Areas mrben) x Land Use Residential: SIngle Famlly A - k - C .40 -4s .so I@, Multi-Units .45 .50 .60 hTobile Homes .I5 .50 -5s " - Rursl (lots greater than 1/2 acre) .30 .35 .4c .70 .75 .86 Industrial (2) .80 .85 -90 I 90% Impewlous H1.R. H. B -35 = - -SHEET NQ. OF - i- I L KKED DATE JOB JOB NO. Description Area CA) 1,709 Ac. a6rf Referonce ~OtFrICIrNT OF RUNOff: C (conolder probable development) peveloped Areas (Urban) lc land Use Rerldcntial: - A k E e Single Fnmlly 1. I/o Multi-Unitr Mobfie Homes .40 .45 .so .55 - .45 .so .60 @- .45 .so -55 .65 = Commercia! (2) 80% Impewlous [ .- Industrial (2) \ 90% Impewlous TIME or CONCENTWTION~C (Cbn B-1) Hi .R. si. b.R. L. .70 .75 . BO -85 6 -80 .85 -90 .95 = l= Dlrtanoe in Miles H= Height In Feet I I I I I I I ~LrrlCIrNT Or RUNOFF: C (conrlder pmbble development) peveloccd Areas (Urban] x land Use Cwff Soil Typ: ( 1) iclent " C " Residentlal: Single Family I VU Multi-Units Mobile Homes .45 .45 .so .60 .so -55 -65 = - R-1 (lots greater than 1/2 acre) .30 .3s -40 .45 = - Commercia! (2) 80% Irr,pervlous tr Industrial (2) 90% Impemlous .70 -75 -80 .85 = - .80 .85 .so .95 = - I!- 'KED DATE JOB JOB NO. pVTlClENT Or RUNOTT: C (conrlder probnble development) Developed Areas (Urban) % Lsnd Uce Coefficient C n boil Type ( I) Resldenthl: Single Family Multl-Un$ts .45 .so -60 .70 = - hqoblle Homes .45 .so -5s .65 = - I * R~I (lots greater than I/Z acre) .30 .35 .I@ Commercia! (2) 80% Impervlous (- - Industrial (2) 90% Impervlous .70 .75 -80 .85 = - .80 .85 -90 .9s = - la.??. L. L= Dlrtance in Mller H= Helpht In Feet HY DROLOCY CkLCULATlONS - RAT#@WAL MLTHOD- SHEET NQ. OF - DATE JOB JOB NO. ~EFFlClrNT Of RUNOrF: C (conrlder probable development) peveloped Area6 (Urban) x Land Use Slngle Famlly Multl-Unlts -40 -4s .5D .55 - - .45 .so -60 .7G = - hqoblle Homes .45 .50 * 55 .65 = - UC, Run1 (lots greater than 1/2 acre) .30 .35 .4D @- Commercia! (2) 80% Impervious t- Industrial (2) - 90% Impervious . 70 .75 -80 .es = - .BO * 85 .90 .95 = - L= Dirmnce in Miles H= Height In rcet BY DATE SHEET NQ. OF - C, KED (- DATE JOB JOB NO. ~OLFilCIrNT OF RlJNOrT: C (conrider probable development) A E - C E .40 .IS .so .55 = - Multi-Units .45 .so .60 .7G = - Mobile Homes .45 .so -5s .65 = - I@ Rml (lots greater than 1/2 ecre) .30 -35 .ID @= o.y/ Commercia! (2) 80% Impervlour i- - Industrial (2) 90% Impervlous .70 -80 .75 .80 .85 = - .85 .90 .95 = - L= Dlrance in Miles H= Helght In Feet % Lsnd Ute Residential: A k Single Famlly -40 .45 Multl-Unlts .45 . so h40bile Homes .45 .so 46. (f RUR.I (lots greater than I/Z acre) .30 .35 Commercial (2) .70 .75 80% Impervious - 3 .L Industrial (2) .60 .65 90% Impervlous G .so .60 .55 -40 f eo .90 e .55 - - .95 = Form by; A.N. L. XKED DATE JOB JOB NO. Description AreaCA) l.Ot Ac. pEFflCIENT OF RUNOFF: C (connlder probable development) pevelo~ed Area6 (Urban) x Land Use Residential: A s - C P Slngle Famlly Multi-Units .40 .45 .so .s5 - -45 .so .60 .?G = h4obile Homes .45 .so -55 -65 = l(P RWZI (lots greater than 1/2 acre) .30 -35 .4@ -45 = qJ Commercia! (2) (- 8045 Impewlous Industrial (2) 90% Impervious nME OF C0NCChTfUTIOh"fC (Chart 8-11 HI.?%. n. b.R. L. . 70 .75 . eo .E5 = - .eo .E5 -90 .95 = - L= D16tanM In Miles H= Hclght in Feet Form by: A.U. HY DROLOCY C&CULAllONS - RATlHIRL MC7HOD- SHEET NQ. OF - CL .KED JOB JOB NO. ~OrrFlCIrNT OF RUNOTT: C (conmldrr probable development) pevelomd Areas (Urban) x Land Use Residential: A Slngle FamIly .40 .45 .SO' .5s - - ,J~Q ~ultl-unltr .4s .so .60 @=.3 hqobile Homes .IS .so .55 -65 = - Rwcl (lots greater than 1/2 acre) .30 .35 .4c -45 = __ - Commercia! (2) 80% Impervious (," Industrial (2) 90% lnpervlous HI .R. H. L.R. 1. .70 .eo -75 .eo .B5 -90 % .. \- 1- , ,- 1- ., I- . (- j .- i' 1 ~ .. .. ." j .,.~ ... ... ... L c . , XKED DATE JOB JOB NO. Description "A% AreaCA,! /.L4Z. Ac. FOErrICIENT OF RUNOTT: C (conrlder probable development) peveloved Areas (Urban) 96 Land Use E w'f So11 Type ( 1) ictent C " Residential: Single Family h B - C .. 40 -45 .so .s5 = !d Multi-Unitc .45 .so .60 @- hqobile Homes .45 .50 .Sf -65 = - Rwel (lots greater than 1/2 acre) .30 .35 .40 -45 = - Commercia! (2) 80% Impervious (- Industrial (2) 90% Impervious b.R. L. .70 .75 . eo .85 = - .eo .85 .90 .95 = - L= Distance ln Miles H= Height In Feet pr DATE SHEET NQ. OF - c CKED DATE JOB JOB NO. FOEFTICIENT OF RUNOTr: C (conmfder probable development) peveIoDcd Areas Wrben) % Land Use Resldenthl: - A k E Slngle Famlly -40 .IS .so : .5s - /pJ Multi-Units .45 .so .60 & hTobile Homes .45 .so -5s .65 = Rml (lots greater than 1/2 acre) .30 .35 .40 -45 = - Commercia! (21 80% Impervious !- - Industrial (2) 90% Impervious H1.k. H. .70 .75 80 .BS = - .BO .85 .90 .95 = HYDROLOGY CALCULATIONS - RATtOUAL METHOD- SHEET NO. OF - C .[KED DATE JOB JOB NO. Description AroaCA) 3.2 x3 Ac. Reference WrrS7CIENT Or RlJNOrT: C (conrldcr probable dcvclopmcntl peveloped Area6 [Urban) x Land Use RerIdentLsl: - A k - C E Single Famlly -40 .45 -50 .55 = Multi-Unltt .45 .50 .60 @- hTobile Homes .45 .so * 55 .65 = RLIR.~ (lots greater than 1/2 acre) .30 .35 .40 .45 = - Commercial (2) 80% Impenriour (- Industrial (2) 90% Impervious h!E Or COh’CChTRSfl0h”C (Chan B-1) Hi .Pt . H. U.R. L“ .70 -75 -80 .85 = .eo .85 -96 .95 = L= Dlrtance ln Miles H= Height In Feet FOtFFlCIENT OF RUNOrr: C (conrlder probnble development) peveloped Areas (Urban) % Land Use Residential: Slngle Famlly Multi-Units hfoblle Homes r-w RUYL~ (lots greater than 1/2 acre) Commercial (2) E@% Impervlous f- ff Industrial (2) 90% Impewlour C=ff Soil Typ ( 1) icienr * C " - A k - C .40 .45 -50 .45 .50 .60 .45 .50 -55 .30 .35 .40 .70 .75 * 80 -80 .E5 -90 L= Dlsrance ln Mlles H= Hclght In reel 2 .55 - - .7G = - -65 = - .45 = .BS = - .95 = * ~trrIClENT OF RUNOrT: C (conalder probable development) peveloped Areas (Urban) % Lsnd Use Soil Type ( 1 ) Epcfficient *' C Residential: - A B - C Slngle Family -40 .45 . so .ss - 1" Multi-Unttc .45 .so .60 @a hqobile Homes .45 .50 -5s .65 = - Run1 (lots greater than 1/2 ncre) .30 .35 .4D .45 = - Commercia! (2) 80% Impewlous 1- Industrial (2) 90% Impewlous .70 .75 .so .85 = - .BO .85 .90 .95 = - Descriplion Descriplion /l'iL - Referwe FOLrFICIENT Or RUNOFF: C (conrlder probnble development) peveloped Area6 (Urban) x land Use Resldcntbl: Single Famlly 71.29 Multi-Units .4s .50 .60 Mobile Homes .45 -50 -55 2g.71 Rw~l (lots greater than 1/2 acre) .30 .35 .40 Hi.R. H. .70 .75 .eo .BO . BS .90 L= Dlrance Ln Miles H= Height In Feet .E5 = .95 = WEFFICIENT OF RUNOFF: C (conrlder probable development) pevelo~td Area6 (Urbsn) x Land Use Reridenthl: Slngle Family q7.i' Multi-unlts h9obile Homes fl,.lf Run1 (lots greater than 1/2 acre) Commercial (2) 80% Impervious ,- Industrial (2) I 90% Impervlous HI .PI. H. b.R. L. A E - C E .40 .4s .so ' .55 - -. .15 .so .60 & .30 .35 -40 &)=E .45 .so .55 .65 = - .70 .75 . eo .85 = - .eo .85 .90 .95 = " L= Dlrtance ln Miles H- Height In reel RV L.VAT.t - SHEET NQ. L- OF - KKED DATE JOB JOB NO. ptFFICIENT OF RUNOFF: C (conalder pmbmble development) peveloped Are86 (Urban) 96 land Ute Residential: Single Family I@ Multi-Units Mobile Homes h -40 .45 B .45 -50 .50 -60 - .45 .50 -55 .65 = - Run1 (lots greater than l/Z acre) .30 -35 .40 .45 = - Commercial (2) 80% Impervious G Industrial (2) 90% ImpervIous H1.R. H. h.R. L. .70 .75 -80 .e5 = - .EO .85 -90 .95 = - ResIdential: - A B - C Slngle Family .40 -4s .so /Lp Multl-Unltr .45 .so .60 Mobile Homes .45 .so -5s ~~21 (lots greater than 1/2 acre) .30 .35 .40 Commercia! (2) 80% Impervlous ( -- Industrial (2) 90% Impewlous .70 -75 .80 .80 .85 -90 E .55 - __ .65 = -45 = - .85 = - .95 = - PV i- ~ ~~ DATE. SHEET NQ. OF - CCKED DATE JOB JOB NO. WErrICILNT Or RUNOFF: C (conrlder probable development) peveloDed Areas (Urban) % Land Use Residential: A B - C B Single Family .40 .45 .so ' .5s = - Multi-Units .4s .so .60 .70 = - Mobile Homes .4s .50 .5s -65 = - ~unl (lots greater than 1/2 scre) .35 .4D .45 = - Commercia! (2) .75 . a0 .85 = - 80% Impenrlour L- Industrial (2) .85 .90 .95 = - 90% Impervious DME Or COF;CCNTRATIONTC I (11 .LfL31)'k):o c =- 6.7J (Cbn B-1) ni .R. H. IC= time in .minutes L.R. L. H= Height ln Feet L= Dlcmnce ln Miles . PV DATE -. SHEET NO. OF - !- C ;KED DATE JOB JOB NO. FOEFTICSEXT OF RUNOrr: C (conrider probable development) Developed Area6 (Urbsn) x land Use Rerldential: - A B - C B -40 -45 .50 .55 - .45 .so .60 a (7 Mobile Homes .45 .50 .5s .65 = Run1 (lots greater than 1/2 acre) .30 -35 .4@ -45 = Commercia! (2) 80% Impewious I- Industrial (2) 90% Impervious H1.k. n. La.pt. L. .70 .75 . SO .E5 = .SO . E5 .90 .95 = FOEWICILNT Or RUNOTr: E (consider probebk developmen0 peveloped Areas (Urban) % Land Use Coefficient ‘I C 6011 Type ( 1 ) Residential: Single family Jfl Multl-unitr .45 .so .60 7G = - hfoblle Homes .45 .so .Sf .65 = - R~I (lots greater than 1/2 acre) .30 -35 .40 .45 = - \t ’ .70 Commercial (2) 80% Irr,pervlous f- Industrial (2) I 90% lmpervlous DWE Or COh’CCNsRkTSON’~ (Chatt 8-11 H1.R. H” .70 .75 -00 .e5 = - .eo .85 -96 .95 = - b.R. L= Distance ln Miles H= Height ln Feet WEfFICILNT Of RUNOrF: C (conolder probable development) peVelODed Areas (Urban) % Land Use Residential: A B - C &> Slngle Family -40 .45 .so ’ .55 - ” 10 Multi-Units .45 .so .6D p~) = 4.73 Mobile Homes .45 .so .Sf .65 = - Rml (lots greater than l/Z acre) .30 .35 .4D .45 = - Commercial (2) 80% Impervious u- Industrial (2) \ 90% Impewlous TIME Or CONCLhTFKTIOh’TC (Chan B-1) €I1 .R. w. .70 .75 -80 .EO .BS -90 .95 = - L= Distance ln Mlles f6.R. L. H= Height In Feet TC- min hr (10 min. rninmm) . - FOtrFICTLNT OF RUNOFF: C (conrider probable development) pevelo~ed Areas (Urban) % Lsnd Use c -ff So11 type ( I) iclent " C " Residential: A k - c Single Family .40 .IS .so .55 - E 1 / Multi-Vnits Mobile Homes Run1 (lots greater than 1/2 acre) Commercia! (2) 80% Impervious ' Industrial (2) 90% Impervlous ph!E Or CONCCh7FUfIONTC (Chsrt B-1) Hl .F't . H. b.R. L. .45 .50 .60 .70 = - .45 .50 * 55 .65 = .30 .35 .40 -45 = .70 -75 . 80 .85 = .eo .85 .90 .?5 = L= Dlstance ln Miles H- Height In reet pveloped Area6 (Urben) x Land Use Resldenthl: Single Famlly / d Multi-Units hqobile Homes Rwe.1 (lots greater than 1/2 acre) Commercial (2) 80% Impervlous L. - Industrial (2) 90% Impervlous H1.R. H. U.R. L" coeffielent '' C " 8011 Type ( 1 ) - A B - C -40 .45 .50 .45 .50 -60 .45 .50 .Sf .30 .35 .4G .70 .75 . eo .80 .85 -90 L= Dlrtanoe Ln Miles H= Height in Feet .55 __ B- .95 = - ~rrrlCIENT Or RUNOFF: C (conrtder probnble development) pevelopcd Areas (Urban) x Csnd Use Coefficient C 6011 Type ( 1) n Residential: h B - C E Slngle Family Multi-Units h4oblle Homes -40 .45 *so -55 = - .45 .SO .60 ~- .45 -50 .55 .65 = - R-1 (lots greater than 1/2 ncre) .30 .35 .40 .45 = - Commercial (2) 80% Impervlour f',- - Industriel (2) 90% Impervious .70 -75 . eo -85 = - .eo .85 -90 .95 = - BY DAlE SHEET NO, C .[KED DATE JOB JOB NO. (,- ~OLTrIClENT Or RVNOrr: (conelder probable development) peveloDed Areas (Urban) 96 Land Use Goelfielent '* C * Soil Type ( 1) Resldentlal: A B - C E SIngle Fsmlly Multi-Units Moblle Homes -40 .45 -50 .55 - .45 .50 .60 a .45 .so .5s .65 = Run1 (Jots greater than 1/2 acre) .30 .35 .4@ -45 5: Commercia! (2) .70 .75 .BO .85 = 80% Impervious Industrial (2) 90% Impewlous H1.R. H. L0.R. L. .BO .e5 -90 .95 = L= Distance ln Mlles H= Height ln Feet ~tFTICIrNT Or RlJNOTT: C (conslder probable development) peveloDcd Areas (Urban) - x pnd Ute Resldentlal: h k - C - Single Famlly .40 .45 . so .55 = - Multl-Unlts .45 -50 -60 hjoblle Homes .45 .50 .ss .65 = - RurrI (lots greater than 1/2 acre) .30 .35 .40 -45 = - - @- Commercia! (2) ED% ImpentIous P- .- Industriel (2) 9D% Impentlout Hi .R. €I. b.R. L. .70 .75 . eo .85 = - .80 .85 .so .95 = - L= Distance tn Mller H= Height in het WrFrICIrNT OF RUNOF'S': C (eonrider probable development) peveloDed Areas (Urban) (b pnd Use - Coefficient C .* 6011 Type ( 1) Restdenthl: h k E B Single Famlly -40 .I5 .so .55 - Multi-Units hfobile Homes Run1 (lots greater than 1/2 acre) Commercial (2) - - 80% Impervious I Industrial (2) \ 90% Impervious ME or COKCENTRATION~C (CbR 8-1) Hi .R. H. b.R. L. .IS .so .60 .fG = .45 .so -55 .65 = .30 -35 .40 .4s = .70 .75 . BO .BS = .BO .B5 .90 l= Distance ln Mlles H= Height In Feet peveloped Areas (Urban) x Land Use Soil Type ( 1) soefficient 'I C * ResIdentIal: - A B - C Single Famlly .40 -45 .so .s5 - I& Multi-Units .45 .SO .60 @ Mobile Homes .45 .SO .55 .65 = Run1 (lots greater than 1/2 acre) .30 .35 .40 .45 = Commercia! (2) 80% Impenrious i - Industrial (2) 90% Impervious ME Or CONCEhTR4T.IONTC (Cbn B-1) HI .kt. H. U.R. L. ~ ~. .70 .75 . SO .e5 = .eo . e5 .96 .95 = L= Dlsmnce ln Miles H= Height In Feet FOEFFICTLNT OF RUNOFF: C (conrlder probable development) peveloped Areas (Urban) x Lsnd Use Resldential: A B c C Single Famlly -40 .45 .so id Multi-Units .45 .so .60 h4obile Homes .45 .50 .5s Rum.] (lots greater than 1/2 acre) .30 .35 .4D .70 -75 . eo .eo . e5 .90 L= Dlrtance ln Miles H= Helqht in rcet .55 = .65 = -45 = .e5 = .95 = I LkCKED DATE JOB JOBNO. 7f( ~rrFYCTrNT OF RUNOFT: C (constdcr probable development) peveloved Area6 (Urban) x land Use C=ff 6011 Type ( 1) icient C Single Family I Multi-Units -40 -4s .so .s5 - .45 .SO .60 @=- htobile Homes .45 .SO .55 .65 = Rml (lots greater than l/Z acre) .30 .35 .40 .45 = Commercial (21 80% hpervlous (" Industrial (2) 90% Impervious TJME or CONCCNTFKTION~C (Chart 8-11 H1.R. H. .70 -75 .eo -85 = .BO .B5 .90 9s = GOEFFICIENT OF RUNOTF: C (conmlder probable development) peveloDed Areas (Urban) % Land Use Residential: - A k - C Single Famlly -40 .4s .so Multi-Units .45 .so .60 hqobile Homes .45 .50 .55 Run1 (lots greater than 1/2 acre) .30 .35 .4D Commercial (2) 80% Impervlous (- Industrial (2) 90% Impenriaus Hi .Pt . 331.. D Lo .PI. 5 L. J-rzc' .70 .75 - 80 .BO .85 .90 L= Distance ln Miles H= Height In het .7G = .65 = .45 = .85 = .95 = pevelorwd Areas (Urban) % Land Use Ufficlent " C 6011 Type ( 1 ) Resldential: A k E B d Single Family .40 .45 -50 -55 = 0,J-J- Multi-Units .45 .so .60 .7G = Mobile Homes .45 .50 .55 .65 = R-I (lots greater than 1/2 ecre) .30 .35 .4@ -45 = Commercial (2) i - 8@% Impenrious Industrial (2) 90% Impervlous Hi.R. n. L0.R. L. .70 .75 .eo .85 = .80 .85 -90 .95 = FOEFFICILNT OF RUNOrT: C (conrlder probable development) pveloped Area6 (Urban) x Land Use Soil Type ( 1) Epcfficlent C " Resldentlsl: - A B - C !fl Slngle Famlly -40 .4s .so Multl-Unlts .45 .so .60 Mobile Homes .45 .so * 5s Rwzl (lots greater than 1/2 acre) .30 .35 .40 Comnercia! (2) E@% Impenrlous r" Industrial (2) 90% Impewlous TIME Or CONCChTRAT1ONTC (Cbn B-1) Hl.Pt. n. b.R. L. .70 .75 .80 .eo .85 .90 L= Distance in Miles H= Height In Feet .7G = .65 = -45 = .85 = .95 = I- (" .. .. .. .. ! ~ , 1 .c manlTOUonolnorrlng compsny HY DROLOCY ChLCULhnONS 1,o * 1,. ...*". I,,."*.*. C.1,1.,",. 1101s l.I.,*.". 1b1.1 Pal 1.11 ',.,I ."*,"..'1". .*'..,'", ,I.""&"* - aArmwm MSTHOO- 8 '- VATt CHECKED DATE JOB JOB NO. SHEET NQ. OF - (. ptrFICIrNT OF RUNOFT: C (conBldcr probble development) pveIo~cd Areas (Urban) Coefficient C " x Land Use Residential: Slngle Family Multi-Unlts hlobile Homes .!M Rwzl (lots greater ~or~rnercisl (2) i " E@?& lrr.penr1ous Industrial (2) \ 90% Impervious Hi .R . )I. b.R. L. .45 .30 .60 .7G = .45 .so .Sf .65 = .30 .70 .75 -80 .E5 = - .eo .B5 -90 .95 = - L= Distance in Miles H= Height In Feet Form by; A.U. CHtCKED Dcscriplion ha CA,! J, L 7L Ac. \ DATE JOB JOB NO. 10s Q WtFFICTLNT OF RUNOTT: G (conrlder probable development) pevelomd Area6 (Urban) % Und Use Rerldential: A B E - Single famlly .40 .4s .so Multi-Units .45 .so .60 hqobile Homes .45 *so -55 Run1 (lots greater than 1/2 acre) -30 -35 .40 Commercia! (2) f- 80% Impervious Industrial (2) 90% Impervlous -70 .75 * a0 .eo .85 .90 L- Distance in Miles H= Height In Feet P .55 - - .95 = - x land Ute Residentbl: A k Slngle Family -40 .4s Multi-Units .IS .so hqobfle Homes .45 .so Rur+l (lots greater than l/Z acre) .30 .35 Commercial (2) .70 .75 ( " 80% Irr,pewlour 1 va Industrial (2) -80 .as 90% Irnpervlous E -50 -60 .Sf .40 eo .so L= Distance in Miles ?I= Height in Feet .ss - - .7G = - .6S = - .45 = - .85 = - ~tFS'lCIrNT OF RUNOFF: C (conrlder probable development) pveloped Areas (Urban) x bnd Use I;gcfficltnt *' C Soil Type ( 1) .I Resldential: A k - C E Slngle Family .40 .45 .so .ss.- Multl-Units .45 -50 -60 .7G = Mobile Homes .45 .50 - 55 .65 = - ~d ~urt?~ (lots greater than 1/2 acre) .30 .3s .40 Commercial (2) BD% lrr,pewious Industrial (2) 90% Impewlous (Chsn B-1) Hl .R. H. .70 .75 . BO .e5 = - . BD .85 .so ,95 = - b.R. L. L= Distance in Miles H= Height In Feet L..cCKED DATE JOB JOB NO. Description AreaCA) 1. '37oYAc. rpt It Basin Referewe GOLrrlCIrNT Or RUNOFT: C (conrlder probable development) pevelo~ed Areas (Urban) x Land Use Residential: Single Famlly Industrial (2) 90% Impentlour A B - C P -40 .45 .so .s5 = .IS .so -60 .?G = .45 .so * 35 .65 = .30 .35 .40 &5L I Yl .70 .75 . BO .8S = .ED .85 -90 .95 = FOTTFICIENT OF RUNOFF: C (conrlder probable development) peveloDrd Areas (Urban] % Land Vre Residential: Single Family Multi-Units Mobile Homes Rml (lots greater &an 1/2 acre) Commercial (2) (- 80% Impervious Industrial (2) 90% Impentlous Hi.&. H. b.R. L. h B - c .40 .45 .30 .45 .50 .60 -45 .50 -55 .30 .35 .4@ .70 .75 .80 .eo .85 -90 L= Distance ln Mllcr €I= Helpht In Fret P .55 - - .65 = .45 = .BS = .95 = - pEFrlClrNT Or RUNOTT: (conolder probble development) pevelo~ed Areas (Urban) x Land Use so11 Type ( 1) coeffieienc C Residentlal: h B - c P * Slngle Famlly .40 .IS .so .ss - ?Xulti-Unlts Mobile Homes .IS .so .60 R-I (lots greater than 1/2 acre) .30 .3s .40 .45 = - Cormercial (2) ( - 80% Impentiour Industrial (2) 90% Impentlous .70 -75 . 80 .85 = - .80 .85 -90 .9s = - b.R. L. L= Dlrtance in Miles H= Helght in €=et Resldentisl: - A B - C E Single Famlly -40 .45 .so .ss ?dultl-Unltr .45 .so .60 .7G = Mobile Homes .45 .so .5s .65 = RWZI (lots greater than 1/2 acre) .30 -3s .4@ .45 = Commercia! (2) (- 804; IrrAperwlous /tu Industriel (2) 90% Impemlous n1.R. H. b.R. L. .70 .75 .80 .E5 = - .eo .85 .9b L= Dlctann in Mlles €3- Height in feet P' DATE -. SHEET NO. OF - ChtCKED DATE JOB JOB NO. 7Y47 Descriplion &ea (A) Y.IL1 Ac. pOErFlCIENT Or RUNOF'r: C (conrider probable development) peveloned Ares6 (Urban) x Lsnd Use Resldentisl: ,/I.' Single Famlly Multi-Units h4obile Homes Rml (lots greater than 1/2 acre) Commercia1 (2) (- E@% Inpervlous Industrial (2) 90% Impervlous H1.R. H. L3.R. 1" A B E -40 .45 .so .IS .so .60 .7G = .45 .so .Sf .65 = .30 .3s .4@ .45 = .70 .75 * 80 .85 = .BO .85 -90 .95 = ChrtKED DATE ' JOB JOB NO. ~EFS'ICTENT OF RUNOS'T: (conelder probble development) pvelo~ed Areas turban) x Lsnd Use Resldential: .A k C Single Famil9 .40 .4s .50 Multl-Unlts .4s .so .60 hfoblle Homes .45 .50 .5s Rum1 (lots greater than 1/2 acre) .30 .35 .40 - Commercia! (2) 8D% Impervlous (- Industrial (2) 90% Impervlous H1 .R. H. .70 -75 -80 .80 .85 .so E .7G = .65 = -45 = .85 = .95 = b.R. L. L= Distance In Milts H= Helght In Feet ChrCKED DATE JOB NO. peveloped Areas (Urban) x Land Use Residentisl: - A B - C tu Single Famlly Multi-Unfts hqobile Homes -40 -4s .so .45 .so .60 .45 .so -5s Rml (lots greater than 1/2 acre) .30 .35 .40 Commercial (2) 80% Impenrious (- Industrial (2) 90% Impewlout H1.R. H. L0.R. L. .70 .75 -80 .80 .85 -90 L= Distance In Miles H= Height in Feet P .7G = .65 = .45 = .85 = .95 = GOLFFICILNT OF RUNOTr: C (conrlder pmbnble development) peveloped Areas (Urban) G-ff1 . f= nt .t .* x tand Use Resldentlsl: A B - C 6011 Type I 1) i /A Single family -40 .45 .so Multi-Unlts- .45 .so .60 .7G = - Mobile Homes .45 .so .s5 .65 = Run1 (lots greater than 1/2 acre) .30 .35 .40 .45 = Commercia! (2) 80% Impewlous r Industrial (2) 90% Impervious I. /bo3 .70 .75 -00 .8S = .80 .85 -90 -95 = I I 1 I I I I FOLTTICTENT OF RUNOFF: C (conrlder probable development) pvelomd Areas Nrban) % Land Use Resldential: - A B - C ici, Single Family -40 -45 .50 Multi-Unlts .45 .50 .60 Mobile Homes .45 .so .55 RLU-ZI (lots greater than 1/2 acre) .30 .3s .4@ Commercial (2) 80% Impervious (* - Industrial (2) 90% Impervious nh!E Or COXCChTRkTIONTC (Chart B-1) HI .R. n. L0.R. 1. .70 .75 . eo .80 .85 .so L= Dlrance ln Miles H= Height In Feet P .55 = /ld .7G = -65 = .45 = .85 = .95 = PLWICILNT OF RUNOFT: C (conmlder probable development) peveloDed Areas (Urban) 96 Land Use Residential: Single Family U .40 .45 .so .55 - - j I& ~ulti-~~nlts .45 .so .60 h4oblle Homes .45 .so -55 .65 = - Run.] (lots greater than 1/2 ecre) .30 .35 .4@ .45 = - Commercia1 (2) I - 80% hpervlous Industricl (2) 909. Impewlous H1.R. - -. H. I0.R. L. .70 -75 -80 .85 = - -80 . E5 * 90 .95 = - L= Dlrtance in Miles W= Height in reet I I I I t I I I I I I CHtCKED DATE JOB JOB NO. Iwr, Description AreaCA) 4.%6/7 Ac. 8am Ucferrnce h5oblle Homes .45 .so .55 R~I (lots greater than 1/2 acre) .30 -35 .40 Commercia! (21 li - 60% Irr,penrious Industrial (2) 90% Impervious DKE Or COh'CEhTRkTION'C (Chan B-1) H1.R. H. b.R. L. .70 .75 . eo .eo .65 .so I.= Dlrtance ln Miles H= Hclpht in Feet .65 = .45 = .BS = - -95 = - HY DROLXY CkLCULATlONS - RATINAL MSTUOD- SHEET NQ. OF - ChAKED DATE JOB JOB NO. Residential: A B - C Single Family -40 .4s -50 .55 - - !u"' Multi-Unftr .45 .so .60 @= - Mobile Homes .45 .50 .35 .65 = - Rml (lots greater than 1/2 acre) .30 .35 -42 .45 = - Commercia! (2) 80% 1rr.pewlous f" Industriel (2) 9D% Inpewlous H8.R. H. L0.R. L. .70 .75 * eo .e5 = - L- Distance in Miles H= Height In rcct FOLFrlCIENT OF RUNOFF: C {conmldcr probable development) pveloped Area6 (Urbeh) x1 Land Use Coefficient " C " 6011 Type ( 1) Residential: Slngle Famlly A k - C -40 .45 -50 .5s = - lyb Multi-Unlts .45 .so .60 & - hqoblle Homes .45 .50 -55 .65 = - Rursl (lots greater than 1/2 acre) .30 .35 .4c .45 = - Commercia! (2) r .- 80% hpervlous Industriel (2) 90% lmpervlouo H1.R. H. b.R. L. .70 .75 . 80 .85 = - Ch-. KED '. DATE JOB JOB NO. 7W Description AteaCA,! 4 LW Ac. 80 sir) Uefenznce Single Family lm Multi-Unlts -40 .IS -50' .55 - - .45 -50 .60 hqobile Homes .45 .so 5s .65 = - Rw~l (lots greater than 1/2 acre) .30 .35 .4c .45 = - Commercia! (2) E@% hpervious (-- Industriel (2) 90% Inpewlous ', nh!E Or COh'CfhTRATIOXfC (ChaK 8-1) H1.R. H. Lo.?%. 1. .70 .75 .80 .85 = - -80 .85 -90 L= Distance ln Miles ?I= Height ln rcet Form by: A.U. pevelo~ed Areas (Urban] % Lsnd Use Coefficient " C " Soil Type ( 1 ) Resldentk.1: A k - C E Single Family .40 .45 .so .s5 - Multi-Unlts .4f .so .60 .7G = hqobile Homes .45 .so * 55 -65 = RUE] (lots greater than 1/2 Bcre) .30 .35 .40 -45 = - Commercial (2) E@%. Impervlous i- I Jb Industrlal (2) 90% Impervlous nh!E Or CONCChTRkTIONTC (Chart 8-11 H1.R. H. b.R. L. .70 -75 . BO .85 = - .80 . 85 -90 L= Distance ln Miles H= Height in Feet Residential: h B - C Single Famlly -40 .43 .so .55 = Multi-Units .45 .so .60 .fO = hqobile Homes .45 .so .5s .65 = /r3 RWCI (lots greater than 1/~ acre) .30 .35 .I@ Commercial (2) 8@% lmpervlous f- Industrial (2) 90% Impervious .70 -75 -80 .85 = .80 .85 .90 .95 = b.R. z?.o L. 75-0 L= DlrtAnce in Mller H- Height In rcct 2 .7f FOEFFICILNT OF RUNOFF: C (conalder probable development) pevelopcd Areas (Urbnn) x Land Use Residential: Slngle Famlly B - C -40 .IS .so .55 = Multl-Unlts .45 .SO -60 .7ti = h3oblle Homes .45 .so .55 .65 = /I?) RWZI (lots greater than I/? acre) .30 .35 .40 Commercia! (2) 80% Inpervious t- Industrial (2) 90% Impenlous H1.R. H. b.R. L. . .70 .75 .80 .85 = .80 .85 .90 .95 = L= Dlstanee ln Miles H= Height In rcet peveloDed Areas (Urban) x Land Use E *if 6011 Type ( 1 ) icient " C " Resldentfal: Slngle Famlly .40 -45 -50 Multl-Unlts .45 .50 .60 Mobile Homes .45 .50 .55 / VD Rurrl (lots greater than 1/2 acre) .30 -35 .40 - A B - C Commercial (2) " 80% Inpervious Industrial (2) 90% Impervious .70 .75 -80 .80 . E5 -90 L= Distance in Miles H= Height in rcct .55 f .70 = .6S = e- ' YJ- .85 f .95 = FOETTICIENT OF RUNOS'r: (conrider probable development) peveloved Areas (Urban) x Land Use Rerldentisl: Slngle Family ~oefficient " C 6011 Type ( I) .40 .45 .50 .55 - Multi-Units .45 .so .60 .7c1 = hiobfle Homes .45 .50 .55 .65 = IUU Run1 (lots greater than 1/2 acre) Commercia! (2) r 80% Irr,pervious Industrial (2) 90% Impervious H1.k. - -. H. .30 -35 .40 @- . 10 -75 . BO .85 = - .BO .85 .90 .95 = - WEFFICIENT OF RUNOFT: C (conrider probable development) peveloved Areas (Urban) Y Land Use Residential: SIngle Famlly Multi-Units Mobile Homes ~3*7 16 R~I (lots greater Commercia! (2) 80% Ir;,penrlous (- "- 7.3 Industrial (2) 90% Impenrlous nm (Chart B-1) Hi .Pt . H. b.R. L. h B - C .40 .45 .so .45 .50 .60 .45 .50 .55 .30 .3s .40 .70 .75 . eo .eo . es -90 L= Dlrtancc In Miles H= Height In het E! .55 = .fG = .65 = .45 = a .e5 = .95 = && c = ,646~ I 7~r Description AteaCA,! 1, /Z f/ Ac. ~OrFFlCWNT Or RUNOFT: C (conolder probable development) pveloped Aresc (Urban) X und Use Residentlal: Slngle Family Multi-Unlts h50blle Homes I,& Rurrl (lots greater than 1/2 acre) CoEmercia! (2) 80% Irr,pewious t- " Industriel (2) 90% Impewlous H1.R. R. L0.R. X.. A B - C .40 .45 .so .45 .50 -60 .45 .50 -5s .30 .35 .4D .70 .75 .eo .80 .85 * 90 L= Distance ln Miles H= Height In rcet .95 f - Developed Ate86 (Urban) x Land Use Residential: Slngle Famlly Multi-Unlts h5oblle Homes C=ff 6011 Type ( I ) iclent ” C “ .45 .SO .60 .7G = - .45 .so .55 .65 = - RWZI (lots greater than 1/2 acre) .3G -3s .4@ .45 = - Conmercia1 (2) 80% Impervious (-- “ Industrial (2) 90% Impervlous H1.R. R. U.R. L. .7G .75 -80 .85 = - .BO .85 .90 @- peveloped Areas fUrbsn] x Lsnd Use Reridenthl: Single Family 6011 Type ( 1 ) wficlent " C " A - B - C P -40 .45 -50 .55 = Multl-Unlts .45 -50 .60 .fG = hqobile Homes .45 .so -5s .65 = Rwl (lots greater than l/Z acre) .30 -35 .40 .45 = Industrial (2) 90% Impervious H1.R. H. b.R. L. .70 -75 -86 .85 = -80 -85 .90 L= Dls~anoe ln Mller H= Height In Feet Developed Areas (Urban) % tsnd Use Residentlal: Single Family A - I! - C E -40 .45 -50 .s5 - Multi-Unlts .45 .50 .60 .7G = Mobile Homes .45 .so -55 .65 = q? Rml (lots greater than l/Z acre) .30 .35 .40 -4 5 = , 2 2 L'J Commercia! (2) 80% Impervious " I Industrial (2) 90% Impervious .70 .75 . eo -85 = .eo .85 * 90 .95 = .YFYI. L0.R. L. L= Distance in Mlles W= Height In rcet ~~~ BY- UATt SHEET NQ. OF - ChtCKED DATE JOB JOB NO. Rerldentlal: - Slnple Famlly Multi-Unlts hqoblle Homes /V3 Rwzl (lots greater than 1/2 acre) Commercia! (21 7. 80% Impemlous Industrial (2) 90% Impemlous H1 .R. . H. b.R. 1. A - B - C B -40 .4s .so .55 - - .45 .SO .60 .7G = - .45 .so -5s .65 = - .30 .3s .40 .70 -75 . EO .e5 = - .eo .85 .9b .95 = - L= Dlrmnce in Miles H= Height In rcet CHtCKED DATE JOB JOB NO. WLFT1CIEh.T Or RUNOTf: C (conrldrr probnblt development) pevcloned Areas Wrben) x land Vre Residential: A B - C E Single famlly -40 .45 I50 .s5 - ~. - htuIti-Unlts h3obile Homes .IS .so .60 & - .45 .50 -55 .65 = - Rw2l (lots greater than 1/2 Acre) .30 .35 .40 .45 = - H1.R. H. L0.R. L. .70 .75 .80 .E5 = - .eo . e5 -90 95 = - Resldentfal: Slngle Family Multi-Unlts h3obfle Homes Run1 (lots greater than 1/2 acre) Commercia! (21 80% 1n;pervlous (r 2) Industriel (2) - 90% Impervious (Chan B-1) H1.R. H. b.R. L. A B - C E .40 .IS .so .ss - .IS .so .60 .fG = .45 .50 .55 .65 = .3G -35 .40 -45 = .70 .75 . eo .85 = .eo .85 .90 L= Distance in Miles H= Helght in Feet CI .KED f DATE JOB JOB NO. @rFrICIENT OF RUNOrT: C (conolder probeble development) peve1oDed Areas (Urban) x Csnd Use Retldtntlal: Slngle Famlly Multl-Units hlobile Homes RLEI (lots greater than 1/2 acre) Commercia! (2) 80% Irr8penrious 'y, d Industrial (2) 90% Impewlous wiclcnt " C .I 6011 Type ( 1 ) .45 .50 .60 .7G = - .45 .so * 55 .65 = - .3G .3s .40 .45 = - .70 .?5 -80 ,es = - .eo .85 .90 pvelopcd Areas (Urban) x Land Use Resldentbl: Single Famlly -40 .45 -50 Multi-Unlts .45 .50 -60 hqobile Homes .45 .so .5s RUI~~ (lots greater than 1/2 acre) .30 .35 .40 A k - C Commercia! (2) 804; Impewious r- Industrial (2) 90% Imperwious (Chan 8-11 H1.R. H. L0.R. L. . '10 -75 .eo .eo .85 .90 B .55 = - .95 = - ptrF'lCIENT OF RUNOTT: C (conrlder probable development) pvelopcd Areas (Urban) x, Lsnd Vre E-ff Soil Type ( 1 ) iclenr " C Resldential: A k - C Slngle Famlly -40 .45 -50 .55 - ___. B Multi-Units .IS .50 .60 .7G = - htoblle Homes .IS -50 .55 * 65 .i. -_. Rml (lots greater than l/Z rrcre) .30 .35 .ID .45 = - Commercia! (2) 80% Impervious r" Industrial (2) 90% Impervlous (Cbn 8-11 H1.R. H. .7D -75 . EO .e5 = - .ED .70 .75 .BD A P E .IO -45 -50 .IS .SO -60 -4 5 .so .65 .3D .3s .40 .70 .75 .6D .. .BO .85 .SO .95 = - 4.71 *$"'. . 1 w '~*-tn br fro.aln.mr .eferencc: Sen Diego County Flood Control Decign and Procedure Menuel 1. Obtmin mail type from Appendice. IX-Cl thru 1x44 . 2. Obtein Prcclpitetion from Appcndicec 1144 thru 114-13 3. 01tein Intensity from Intencity-Duration Dtcign Chart-19B4 Rccldentbl: A L E -40 -4 S .so .70 .75 .8D .eo OB5 . BD .95 - - .. ZC - oh br Iro.m&bmsnloua) I ferencc: San Dlcgo County Flood Control Declgn and Procedure Wnual 1. Obtain moil type from Apptndlcem IX-C1 thru 1x44 . 1. Obtain PreCipitDtiOn from Appcndiccr 114-4 thru 114-13 3. Obtain Intensity Iron, lntcnsity-Duratlon Design Chert-lOBb .7O .75 .bD .e5 .OD -8s = .95 - - .- Slnglc hmlly "- Multl-Unltr %- 10 ah br 10 :fcrcnce: 6an Diego County Flood Control DeciBn an6 Procedure Hmnual 1. Obtain .oil t7pe from Appendice. lX-CI thru ZX-C4 . 2. Obtaln PreclplLatlon from Appendlcec 114-4 thru 114-13 3. Obtain lntcnrlty from lntcnrlty-Duration Dtrign Chert-1984 i.\ ,- 0 "- - N 'W n c . c c '"I +r u c 0 CL 0) c m CI L n W D W +r 0 .W R c. 6-Hour Precipitation (inches)? $78/ /!/u.6 A- / /D-Z7-P;: **C**I****I*****ICI***********U********************************************* - PRESSURE PIPE-FLOW HYDRAULICS COMPUTER PROGRAM PACKAGE (Reference: LACFD,LACRD,& OCEMA HYDRAULICS CRITERION) ............................................................................ ~(<<((((((((<((((((((((((((((((((((((())))))))))))))))))))))>)>>))>))))>)))> (C) Copyright 1982 Advanced Engineering Software [AESI Especially prepared for: MANITOU ENGINEERING COMPANY <(<(((((<(<((((((((((((((((((((((((((()>)))))>))))))))))))))))>>>)>))))>>))) X******X*~**~**~**~*~******************************************************* NOTE: STEADY FLOW HYDRAULIC HEAD-LOSS COMPUTATIONS BASED DN THE MOST DESICjN MANUALS. CONSERVATIVE FORMULAE FROM THE CURRENT LACRD,LACFCD, fWD OCEMA D[W\ISTREAM PRESSURE PIPE FLW CMROL DATA: NODE NUHBER = 515.00 FLOWLINE ELEVATION = 361.12 PIPE DIAMETER(1NCH) = 18.00 PIPE FLW(CFS) = ASSUMED DaJNSTRECIM CONTROL HGL = 362.620 14.70 "-"" "" """"""""_""""""""" """""__ ,- ""- """""""I==- -I"-=== "E"""_""""" PRESSURE FLOW PROCESS FROM NODE 515.00 TO NODE 510.00 IS CODE = 1 i UPSTREAM NODE 510 .OO ELEVATION = 366.92 1 >. CALCULATE PRESSURE FLW FRICTION LOSSES(LACFCD): PIPE FLOW = PIPE LENGTH = 14.70 CFS PIPE DIAMETER = 18.00 INCHES 152.75 FEET WINGS N = ,01200 SF=(Q/K)**2 = (( 14.70)/( 113.797))**2 = .0166867 HF=L*SF = ( NODE 510.00 I HGL= < 365.169);EGL= ( 366.243);FLOWLINE= < 366.920) 152.75)*( .0166867) = 2.549 PRESSURE FLOW ASSWPTION USED TO ADJUST HGL AND EGL LOST PRESSURE HEAD USING SOFFIT CONTROL = NODE 510.00 : HGL= ( 368.420);EOL= ( 369.495);FLaJLINE= ( 366.920) 3.25 ...................................... ...................................... - .................................................................. PRESSURE FLOW PROCESS FROM NODE 510.00 TO NODE 509.00 IS CODE = 5 UPSTREAM NODE 509.00 ELEVATION = 366.92 CALCULATE PRESSURE FLOW JUNCTION LOSSES: ...................................... ..- nr"lr*"r I\.A,.l-l.Cn Aacn I IC, r.Fl7-V ne, TA u1 PRESSURE FLOW PROCESS FRUI NODE 510.00 TO NODE 509.00 IS CODE E 5 UPSTREW NODE 509.00 ELEVATION = 366.92 "3. DISCHCIRGE DIANETER AREA VELOCITY DELTA w I 8.5 18.00 1.767 4.810 4.500 .359 2 14.7 18.00 1.767 8.318 3 0 .o " 1 .074 4 0 .o 0 .oo 0 .oo 0.000 0.000 0 -000 0 .ooo 0.000 0.000 - 5 6.2===05 EQUCILS BASIN INPUT=== CALCULATE PRESSURE FLUJ JUNCTION LOSSES: - LACFCD fWD OCEMCI PRESSURE FLOW JUNCTION FORMULAE USED: DY=(02*V2-Ql*V1*COS(DELTAl)-Q3*U3*COS(DELTCI3)- 04*V4*COS(DELTA4))/((~1+A2)*16.1) UPSTREAM WINGS N = .01200 DOWNSTREAM WINGS N = ,01200 UPSTREAM FRICTION SLOPE = .00558 WERAGED FRICTION SLOPE IN JUNCTION ASSUMED AS .01113 DOWNSTREAM FRICTION SLOPE = .01669 JUNCTION LENGTH(FEET) = 4.00 ENTRANCE LOSSES = .215 FRICTION LOSS = .045 JUNCTION LOSSES DY+HUl-HU2+(FRICTION LOSS)+(ENTRfWCE LOSSES) NODE 509.00 : HGL= < 370.112);EGL= < 370.471);FLMJLINE= < 366.920) JWCTION LOSSES = 1.433t .359- 1.074+( .045)+( .215) = .977 " """""I ~ PRESSURE FLOW PROCESS FROM NODE 509.00 TO NODE 505.00 IS CODE = 1 "" -=e .YPSTREW NODE 505.00 ELEVATION = 367.60 ..................................... LALCULATE PRESSURE FLOW FRICTION LOSSESCLACFCD): PIPE FLOW = PIPE LENGTH = 8.50 CFS 44.64 FEET PIPE DIFIMETER = 18.00 INCHES MC\NNINGS N = .01200 SF=(WK)**2 = (( HF=L*SF = ( 8.50)/( 113.797))**2 = .0055792 44.64)*( .0055792) = .249 NODE 505.00 : HGL= < 370.361);EGL= < 370.720);FLOWLINE= < 367.600) """ PRESSURE FLOW PROCESS FROM NODE 505.00 TO NODE 504.00 IS CODE = 8 UPSTREAM NODE 504.00 ELEVATIMJ = 367.60 PIPE FLOW(CFS1 = CALCULATE PRESSURE FLOW CATCH BASIN ENTRANCE LOSSES(LACFCD): 8.50 PIPE DI"lETER(1NCH) = 18.00 PRESSURE FLOW VELOCITY HEAD = WITCH WSIN ENERGY LOSS = .2*(VELOCITY HEAD) = .2*( .359) = .072 .359 ="-E- ___""" - " """P ....................................... NODE 504.00 : HGL= < 370.792)1EGL= < 370.792);FLMJLINE= < 367.600) ="""""==""-I--""==="----- _I"""""-=~LS=C=CE=~=" END OF PRESSURE FLOW HYDRAULICS PIPE SYSTEM "m% ...................................... """""""""""""""~""""""""""""""""""""""- - ...................................... ~ ~~ ~ ~ ~~~~~~~~~~ ~~~~ ~ ~~ PPECSLIRE FLOil PROCESS FROM NODE 455.00 TO I-IODE 454.00 IS CODE = 5 L1FSTF:EA:I MOUE 454.00 ELE'JATION = 284.73 ~ ~ ~~~ ....................................... C-LCULATE PRESSURE FLUlJ JU.ICT101 LOSSES: AREA VELOCITY DELTG _"""""""""""""""""""""""""""""""""-"""" ...................................... ................................................ C:ALTIULATE PRESSURE FL0)J JUI4CTIOt.l LOSSES: :dbIl. C:I".fHAPGE DIAMETER AREA VELOCIT'r [iELTA HI..! 1 t. 8 . t. 36.00 7.069 9.705 0 .on0 e5.g 3 t. . 0 0 1 .462 7.049 12.13s 3 i7.2 24 -00 3.142 2.25p 5.475 ?0.000 4 0 . 0 0 .no 0 .000 0 .000 u ,000 ., .o===x EDUALS eAs1r.l INFLIT=== i " - c - ....................................... ...................................... """"""""""""""""""""""""""==""""""""""" .......................... PRESSLIRE FLOlll PROCESS FROM NODE 428.00 TO NODE 427.00 IS CODE = 5 LlPSTF:EAIl ViilDE 427 .[I@ ELEVATION = 320.05 """""""""""""~""""""""""""""""""~~"""""- CA!.Cli!.CTE P'F:E"Si.lPF Fi 13.:- JI&!LT.!LlP$ krs?C,F?: - -. -~ - ~ - - - w. DISCHARGE LIAMETER AREA VELOCITY DELTA HO - "" 2 1 23.0 29.6 24.00 24.00 3.142 3.142 7.321 9-42? 0 .0@0 1 .376 ,832 " ....................................... """~""""""~"""""""""""""~"""----------"------""- F'RE:3C.IJRE FL3I:I PROCESS FROM NODE 427.00 TCI I'4ODE 420 .Ut1 IS CODE = 3 UFSTF:EA!l IJSIDE 420 .GC! ELE:!ATIOIJ = 224 .5? 324.590': .................................................. """""""""~"""""""""""""""""""""-----""------ PRESSI-;F:E CLS!.! ~~~CESS ~~gb,: -nri ,,,.,,E 41:?,?3 TC fiO[!E 417.00 IC' CODE = 5 LIPSTREAP! IJCIBE 417.0CI ELE(,.jMTI@pj = 325'.,55 """_ PRESSLIRE FLO!?! PROCESS FRO11 NODE 445.@C TO NO2E 444.00 IC CODE = E UF'STREA;M F4ODE 444,@0 ELEVATION = 302.01 """""_""""_""~""""""""""""""~""""""""""" CALCULATE PRESSURE FLOM CATCH BASIN ENTRA;I<C.E LDSSES!LACFCD) : -.. PE FLOI.<(CFS! = 16,.!0 PIPE DIAMETEPIINCH! = 18.O@ __ ~uF.E~FL~uI'.~~~~~~-~~F~!c~-~,~~~ _____- CATCH BASIN ENERGr LOSS = .?+<VELOC.ITY HEAL!:! = .?X( 1.2891 = .258 NODE 444.00 : HGL= < 3@5.057;L;EGL= < 305.057.~jFLOWLINE= < 302.010) ~""""""""""""""""~ - """"""""_ -------------~"""""""""""~ """ --"--"---"----------~"" "" END OF PRESSURE FLO1.I HYDRAULICS PIPE SYSTEM ~ - ." ~~ ~- - "- - - ...................................... ...................................... PRESSLIRE FLOW PROCESS FROY NUDE 429 .CIO TO NODE 42h .00 IS CODE = 3 CIPSSREAll NODE @[I ELELiATI@I< = 322.4C1 CAI i F!PE FL&! = PIPE LENGTH = 20.417 CFS PIPE DIAMETER = 24.00 INCHES CErdTRk!. ANGLE = 35.700 DEGREES 264.45 FEET rv+rm~tw rd = .OIZOO FLO!?.! VELOCITY = 4.49 FEET PER SECONO PRESSLIRE FLCIIA AREA = 3.142 SOUARE FEET 'JELOCIT"' HEAD = ,655 HB=KB*iVELUCIT'..c HEAD:) = ( .157j*( ,6551 = BEIK! CCIEFFICIENT!KB:) = ,1575 PIPE CCill'JEYAl4CE FACTOR = 245. (176 ,103 FRICTlOt< LOSSES = LxSF = ( 264.45!*( ,00672E3:) = 1.832 ....................................... L,JLATE FRESSLIPE FLCIlnl PIPE-BEt.ID LOSSES!OCEFIA! : FRICTION SL@PE!SFj = .00C9288 NQDE 4'i LL,.OO : HGL= < 320.227:;EGL= < 320.B8?;;FLOIJLII.IE= < 322.4nOj - .................................... LEST PRESSLIRE HEGP USIr.IG SijFFIT [I(I;.!TEOL = PRESSLIFE FLOW kSE.:J!.iPTIC!t,l IJCELI T;! ADJI?ET HGL Ab.;[! ELL 4.17 !,!ODE 426.ClO : HGL= i :?2;.;[![l>,;EGL= .< ~~E,~I~~);FL[II~~L!~..IE.I < 322.406; ....................................... ....................................... UPSTREAil NODE 2086.00 ELEVAT 1 @b! = 342.24 PRESSIURE FL@l.d PROCESS FROM NODE 2@2?.00 TO NODE 2@8t..O? IS CODE = 1 ........................................ CALCULATE PRESSURE FLOW FRIC.TI@N LOSSESILACFCD) : PIPE FLOi:' = PIPE LENGTH = G.60 CFS PIPE DIAMETER = 18.00 INCHES 44.50 FEET MAI4NINGS N = .@120l! HF=L*SF = ( aF=!Q./t:jr+2 = (( G.6O)/i 113.797X!**2 = .ti057113 44.50:1*, .@L75?113:I = ,254 NODE 2086.00 : HGL= < 34h,39t!;EGL= < 34h.763?;FLClWLINE= < 342.24Cli P ....................................... ....................................... PRESSURE FLOG1 PROCESS FRilM NODE ?EiGt,.OO TCi NODE 2085.00 IS CODE = R UPSTREA?! !..!nIlE 20f5.00 ELE!/i;TI OE4 = 342.24 ....................................... ....................................... PRESSURE FLU!: PROCESS FRii4 NODE 427.00 TO NODE 407.00 IS LODE = 1 LIPSTREAM NODE 407.00 ELEI.~IAT] KIN = 320 . 9s CALC'ULATE PRESSURE FLOIj.! FRICTICIN LCiSSESiLACFCD:! : PIPE FLO!,d = 6.40 CFS PIPE PIAHETER = 1'2.00 IKCHEC' PIPE LEbIGTE = 9.25 FEET wrwrm I.: = .c1!200 SF=(Q,,'K)xx2 = (( HF=L+SF = ( 6..50')./( 113.797:;j+fz = .0[!3363'2 NODE 407.00 : HGL= { 323.<SB);EGL= < 323.~,~~,?;FLOl~ILINE= { 320,980'. ...................................... '3.23*( .cic:;?63;:1 = ,031 ...................................... ....................................... PRESSLIRE FLO!.d PROCESS FROM NODE 4i9.00 TO NODE 405.00 IS C.OT!E = 1 L1P'SSREA:I N@DE 405.00 ELEWTION = 324.89 """""""_"_""""""""""""""""""""""""""""" C4l.CLILtiTE PF:ESSlJEE FLO!..1 FFI CTI Ob..! LClSSESiLAC:FC:@, : PIPE FLOil = c d.EO CFS PIPE DIAMETEP = 19.00 INCHES PIPE LEI?GTH = 14.17 FEET 3F=([i,i)-;j*+2 = <( IlkrJNING'S I4 = .0:200 HF=LISF = i 5,9[1j.,/( 1!3.797:!!**2 = .0@2:?77 14.19;Iri .ii02;977:) = , CI 37 NODE 405.0.0 : HGL= < 327.309.);EGL= i j2?.47t;;FLOWL!NE= i 324.8'?0; c """"""_"""""""""""""""~"""""""""""""""" ....................................... PRESSIJRE FLW PROLEGS FR~M NODE 41'7.crcl TU NODE 40?.0c IS CODE = 1 IIFSTFEAVl NODE 4i'9.00 ELEVAT1Cli.l = 324.78 CALCLlLATE PRES6URE FLfi,d FR1CTIOE.J LDSSES!LACFCD:): FiPE FLOV = 3.70 CFG PIPE LEXETH = 55.25 FEET MANNING:; N = ,01200 """"""_"""""""""""""""""""""""""""""""~ PIPE DIAMETER = 18.00 INCHES SF=(Q/K)++2 = (< HF=L*SF = < I-IODE 40'7.0Cl : HGL= < 327.309;;EGL= < 327.377>;FLOWLINE= < 324.980:) 3.70:)./< 113.7'77:!:)**2 = .0010;72 -.= 3.<.29)x( ,0010572:) = ,037 ...................................... ...................................... PRESSI!RE FLD!,;I PRDCESS FRD:I NODE 4U9.00 TO NODE 408.00 IS CODE = 8 UPSTREAH ~KIDE 408.00 ELE0ATIOt.l = 324.98 """"""_"""""""""""""""""""""""""""""""~ - LCLILATE PRESSURE FLOW CATCH BASIN EI.lTRANCE LOSSES(LACFCDj : FIPE FL@!*1(CFS) = 3.7O PIPE DIAMETEFKINSH? = 18.U0 PRESSLIRE FLOld 'OELOCITY HEAD = .@de CA1C:H BASII.! itJERG"( LCISS = .2i(VELOCIT~( HEfiiD:! = .2X< .0,18! = ,014 NCiDE <[IE.[IO : YGL= i 327,3flqEGL= i: 3~7.3'~f;;FLUI~ILI1-iE= ( 3;4,Ugfi:> El.![. c: F!:';-'Zi.!-!<;'F- F?(l:,I H':[,Fb3l-~!][:, p;Fc i.'c-r'. : i z, ti: ~ """"- ~ """"~""""_""""""""""""""""""""""""""""" ...................................... PRESSLIRE FLOl..(! PROCESS FROi: RODE 4?7.00 TO NODE 534 ,@@ 15 CODE = 1 IJPSTREPfl r.::I[iE 534 , 00 ELEt*JA?I(ii.J = 33b.63 """"""""_"""""""""""""""""""""""""""""- PRESS'JRE FLOL? FRCtCESS FROEI NIDE 5'31 ,130 TO NODE 530 .@Cl IS POCiE = 1 LIPSTRE44 NODE 530 .@@ ELEVATIOH = 353 .E3 "_"""""""""""""""""""""""""""""""""~~""~ CALCULATE PRESSURE FLW FRICTION LOSSESrLACFCD:) : FiPE FLOW = 6.30 CFS PIPE LEI.1GTH = RIFE 5li;METER = 18.00 INCHES ?3.?E' FEET MANXINGS I.i = ,01200 SF=(Q/K)f*2 = i( &.3@),ji 113,?":):!**2 = .OO:;(IdJ? HF=LxSF = i 33.28,*! .@CI306JCj = .102 t.ICl[!E 530.@11 : HGL= i 344.0iS:>;EGL= ; 34J.215i;FLOl,~LiNE= .( 353.S3Ctj ....................................... ....................................... PRESSURE FLOl PROCESS FRO;I NODE 425.00 TO NODE 423.00 IS CDDE = 1 llPSTREtit,l NODE 423.00 ELEI'&T I [ti = 32" I [I [I ........................................ PRESSURE FLOI.:! PROCESS FROM NOPE 423.00 T@ IdilPE 422.00 15 CODE = 8 LIPSTREAII NODE 422 .Ob ELEVfiT1CW.I = 32?.@0 GLCULATE PRESSLIRE FLOI,J CATCH PASIN EI4TRAIJiE LOSSES<LAt.FC.D! : PIPE FLOI.I(CFS:I = 4.40 PIPE DIAIIETEE(IIdCH! = 16.00 ATCH EASIN ENERG'i LOSS = .2+<VELOCITY HEACJ) = .2*( .OS&) = .Dl9 NODE 422.00 : HGL= ( 330.&iA:>;EGL= { 33@.616:;FLMdLINE= { 329.00@> END OF PR€ESSURE FLCIlN HYDRAULICS PIPE SYSTEM ....................................... '"'ESSURE ElLll?l AJ€L@CI~TY HEM-? ~ -.DW~ ~ . ~~ """""""_"" - "" "_. """"""_"""""""""""""""""""""""""""""""~ ,- .- ._ """-""""""""""""""""""""""""""""""""""- ...................................... PRESSIJRE FLOlJ PROCESS FROM NODE lO82.10 TO NODE lC172.00 IS CODE = 1 UPSTF:EHII NODE 1072.00 ELE1~.JATION = 218.21 CALCULPTE PRESSURE FLO!J FRICTION LOSSES!LACFCDj: PIPE LENGTH = 5.25 FEET PI PE FLOG! = 8.00 CFS PIPE DIAMETER = 18.OO INCHES SF=!Q/K:l**2 = (( HF=L+SF = ( ?.25?*< .0045422) = .046 NODE 1C72.00 : HGL= ( 243.700?;EGL= < 244.@lB?;FLOWLINE= < 238.210) ~.oo:L/! 113.797j:)**2 = .Oil49422 wwrdIrm N = .012c10 ---------""""""""""~""""""""""""""""""""""" ...................................... - PRESSgRE FLO1.J PROCESS FROM NODE 1072.OO TO NODE 1072.10 IS CODE = E "STREAM NODE 1072, 10 ELE!,ATION = 238.21 -- """""""_""""""""""""""""""""""""""""" CALCULATE PRESSURE FLOW CATCH eASIr4 ENTRANCE LOSSES!LACFCD! : PIPE FLOI.!!CFS?s = F;.oo PRESSLIRE FLOW 'JELOCITr HE*[! = .318 PIPE D!AIIETEE!I!!CH) = 18.UC CATCH 8ASltJ EtdERVY L(?S$. = .2+iVELOCIT'( HEAD) = ,2*( .>]?I = .@A4 NODE 1072.10 : HGL= .< 244.082);EGL= i 244.081)1.;FLD:JLINE= { 238.21@> ...................................... ...................................... PRESSURE FLOW PROCESS FROM NODE 1070.10 TO NODE 310.00 IS CODE'= 3 UPSTREAM NODE 310 .0@ ELELVAT] or.1 = 258 ,RE: ...................................... ...................................... ......................................... - PIX-&..- I .+ , = ~icJowo!A€"-2'~,!l. !$-WOE = -5"- UPSTREAP NCIDE 31 0.10 ELEVATI Old = 25s -86 ...................................... CALCIILATE PRESSURE FLOb! JUNCTION LOSSES: -YO. DISCHARGE DIAMETER AREA UELOCIT'Y DELTA Hv 1 6.6 18.00 2 1 .7t.7 3.735 45.000 .217 1.767 3 9.054 9.4 18.00 1 * 273 1.767 5.319 90.000 4 0 -0 0 .OD 0 .000 0 .on0 0 ,000 5 0 .0===Q5 EQUALS BASIN INPUT=== 14.n 18.00 " - - LACFCD AND OCEMA PRESSURE FLOW JUNCTION FORMULAE USEL: DY=IQ2*V?-Ql*Vl*COSrDELT~i~-~3+'~3*C@SIDELTA~~- Q~*V~*COSTDELTAJ~:I.~~~A~~A~~~~~.~~ UPSTREW r+wdItm rd = .oi2oo UPSTREAM FRICTION SLOPE = ,00336 DOIJNSTREAPI FRICTION SLOPE = ,131977 AVERAGED FRI ZTI ON SLOFE IN JUNCTION ASSUMED AS .Oil57 JUI4CTIOi.i LENGTHIFEET) = 4.?@ FRICTION LOSS = ,046 DUWNSTREAW tlANN1NCiS N = .n12@@ ENTRAtdCE LOSSES = 0 ,000 JUNCTION LOSSES = DTtH',~l-HV~+(FR!CTIOrd LClSS:!t(ENTRANCE LOSSES! JUNCTION LOSSES = 2.240+ .217- i.273tT .[146)+I O.0@@) = 1.229 NODE 310.10 : HGL= < 262.666?;EGL= < 262.882,;FLOWLI~dE= < 258.880) """"""_"""""""""""""""""""""""""""""""~ ...................................... PRESSURE FLOM PROCESS FROM NODE 310.10 TO NODE 308.00 IS CODE = 1 JJPSTREAM NODE 308.00 ELEVATION = 259.39 - criLC.ULATE PRESSURE FLOW FRICTION LOSSES(LACFCDj : PIPE FLOW = L.60 CFS FIFE LENGTH = 12.82 FEET PIPE DIAMETER = 18.00 INCHES FIANNINGS l::q = .o1zon SF=<Q./K3+*2 = #(( HF=L+SF = < 12.82jr1 .@033638:! = h.L(@:! /T li3.7977!>*+2 = ,0033638 NODE 308.00 : HGL= < 262.70Y:>;EGL= < 262.92L;;FLUi~ilNE= < 259.390) .n43 ...................................... """"""_"""""""""""""""""""""""""""""""~ PRESSURE FLOI,d PROCESS FROM NODE 308.00 TO NODE 308.10 IS CCiDE = E: UPSTREAM NODE 308. 10 ELEVATION = 259.39 """"_"_"""""""""""""""""""""""""""""""" CALCULATE PRESSURE FLOG.! CATCH GASIN ENTRANCE LUSSESTLACFCD) : PRESSUF:E FLOIM VELOCITY HEAD = ,217 PIPE FLDIJ(CFS) = 6.6@ PIPE DIAMETERTINCH:! = 18.00 CATCH GASIN ENERGY LOSS = .2*('JELUCITY HEAD:) = .2*! ,217:) = ,043 NODE 306.10 : HGL= i 262.?69>;EGL= < 262.?6?i;FLOWLINE= < 259,390, END OF PRESSURE FLOLJ HYDRAULICS PIPE SUSTEt.; ...................................... ....................................... .......................................... ........................................... PRESSURE FLOI.*! PROCESS FRO!I NODE 315.00 TO NODE 315.10 IS CODE = R YPSTREAH NODE 31 5.1 0 ELEVATION = 24C.98 - ........................................ c&LCLlLATE PRESSLIRE FLNd CATCH BASIN Er.ITRAr.ICE LOSSES(LACFCC1) : PIPE FLOWICFS:) = PRESSUR: FL0l.d 'VELCCIT"/ HEAD = .2E7 7.60 PIPE DIAMETEF:iINCH! = iB.00 CATCH E:ASIN ENERGY LOSS = .2+!VELOCITY HE&Gj = .2*< .?E?:! = ,@5? NObE >15,1@ : HFL= < 25E.5V&"EGL= I 2:5.5uE!i:FLOI,.,JLINE= < 249.98Ci; """""~""""""""""""""""""""""""""""""""- ....................................... ............................................................................ SF 4~~ /'-Z"BG PRESSURE PI PE-FLOW HYDMULI CS COMPUTER PROGRAM PACKAGE - 'Reference: LACFD,LACRD,& OCEMA HiDRAIILICS CRITERION) *rs****X**XI****X******************************************~**************** ((~((~((((((((i((i(((((((((((((((({(((j??))~)?)?))j}~j?.~))???)?)??:)~?))?)~~~ (C) Copyright 1982 Advanced Engineering Software [AESI Especia.lly prepared for: MNITOU ENGINEERING COMPANY (((((!((((((((((!((i((((((({((i{({{((<)?j~)))??)j:)???j:)j?j?;):)??:))))j;~)?:)??)? *tX*****+X*XI~*****~********************************************I*********** NOTE: STEADY FLOIA HYDRAVLIC HEAD-LOSS COMPUTATIONS BASED OX THE MOST CONSERVATIVE FORrlLlLAE FROM THE CURRENT LACRD, LACFCD, AND NEMA DESIGN MAWJALS. NODE NLIKEER = 1054.10 ASSllMED DOI~dk'STREAM CONTROL HGL = 281 .05C PIPE DIAFIETER<INC.Hi = 1'2.00 PIPE FLOIM(CFS) = 7.00 C1CIWNSTF:EAM PRESSURE PIPE FLOW CONTROL DATA: FLOWLINE ELEVATIO'.! = 284.35 ....................................... ...................................... ............................... """"""""""""""""""""""""""""""==""""""" PRESSURE FLOW PROCESS FROfl NODE 1054.10 TO NODE 2050 .00 IS CODE = 1 UPSTREAM NODE 2050 .0@ ELEUATI or4 = 28s. 11 CALCULATE PRESSURE FLOY FRICTION LOSSES<LAC.FCD) : PIPE FLOW = 7.00 CFS PIPE DIAMETER = 18.00 INCHES PIPE LENGTH = 50.70 FEET tlArmIrm N = ,01200 ........................................ SF=(O/K;!**2 = (( 7.00)./( 113.7?7))**2 = .0037838 HF=L*SF = ( NODE 2050.00 : HGL= < 2411.248?:EGL= < 25.1.4?1>;FL@WLINE= < 285.110) 50.70:)*( .@037838! = .1Y2 ...................................... """""~"""_""""""""""""""""""""""""""""" PRESSURE FLOl..J PROCESS FROM NODE 812.10 TO NODE 810 .00 IS CODE = 1 UPSTREAM NODE 81 0.00 ELEVATION = 312.83 ...................................... ........................................ PRESSURE FLOW PROCESS FROM NODE 810.00 TO NODE 810.10 IS CODE = 8 __ UPSTREAM NOUE 81 0.10 ELElIATlON = 312.83 - ""_"""""""""""""""""""""""""""""""""~ .ALClJLATE PF:ESSCIRE FLOW CASCH BASIN ENTRANCE LOSSESILACFCD) : PIPE FLOLJCCFSS = 6.. 80 PIPE DIAMETER!INCH! = 18.00 PRESSURE FLOlc! VELOCITY HEAD = ,230 CATCH GASIN ENERGY LOSS = .Z*(UELOCITY HEhDi = .2*( .23Q:1 = .04g blODE 810.10 : HCL= ! ?16,13e>;EGL= < 318.13~?;FLOl.JLINE= < 312.820, ....................................... EE.IT, nrr UUCC.CI,Dlz ci n,, u~/r,r,,',,, ,rr r.,r,r *.,,C".' PRESSURE PIPE-FLW HYDRAULICS COMPUTER PROGRAM PACKAGE - (Reference: LACFD,LACRD,& OCEMA HYDRAULICS CRITERIONj *tr****X****************~**ft***********************~~***********~ <((({(({(((((!(((({{{{{({{{({{{{{{{{({???)))>?>:):)))>)j?)))))?)))???)??))))):) (C) Copyright 1982 Advanced Engineering Software IAESI Especially prepared for: MANITOU ENGINEERING COMPANY ({tc{(({((((((ii(<(({({{{{({{{{{{{({{(?}>?>~~????j?j))):)jj;j?>>))??))}?)j))? ****~T*f*F********Y****************I**************************************** FdOTE: STEAD': FLOW HYDRAULIC HEAD-LOSS COMPUTATIONS RASED ON THE MOST DESIGN rlAwALS, CONSERVATIVE FORMULAE FROM THE CURRENT LACRD ,LACFCD, AND OCEMA DOWNSTREAM PRESSLIRE PI FE FLO1.J COtdTROL DATA: NODE NUMBER = 1080.10 PIPE DIAMETER(1NCH) = 18.00 FLOWLINE ELEIJATI ON = 236.45 PIPE FLOW(CFS) = 7 .?[I ASSUPIED D@!.ANSTREA?I COVTROL HGL = 239.886 ...................................... ...................................... ...................................... ...................................... PRESSURE FLOW PROCESS FROM NODE 1080.10 TO NODE 1075.00 IS CODE = 1 UPSTREAM NODE 1075.00 ELE?IATIOid = 238.59 ....................................... PIPE FLDld = 7.90 CFS PIPE DIAMETER = 18.00 INCHES SF=!WKj**2 = < ( 7.?0)/1 113.797i)**2 = .n048194 NODE 1075.00 : HGL= < 240.160);EGL= < 240.47Cl);FLOWLINE= < 232.590) HF=L*SF = ( 54.?8)*< .0048194) = .264 CALCULATE PRESSLIRE FLZW FRICTION LOSSES!LHCFCD:): PIPE LENGTH = 54.78 FEET twmIrm rd = ,01200 ....................................... ...................................... PRESSLIRE FLO1.J PROCESS FROM NODE 1075 -00 TO NODE 1075.1 @ IS CODE = 8 ., UPSTREAM - r4ODE 1075. 10 ELEVATION = 238.53 - .................................... PIPE FLOlb!!CFSj = cHLCULATE PRESSUF:E FLOW CATCH BASIN ENTRANCE LClSSES(LACFCDj : 7 .?0 PIPE DIAMETER(1NCH:) = 18.00 FJOOE 1075.10 : HGL= ( 2d0.532);EGL= < 24C1.532';;FLClI,.lL!FJE= < 238.59Oi CATCH BASIN EI.IEF'G''! LOSS = .2+(UELOC.ISY HEAD) = .2+1 .31W = ,062 PRESSLIRE FLOld VELOCIT'Y HEAD = .31U ........................................... ....................................... -,,-. ^- -.~."-...-.- r. -. . ...,^-.: ... ." -." -. . ***+**,*f++****t+**X+*XZ*C+*f*fX+fil+XZX**********************************~* PRESSURE PIPE-FLOW HIDRAULICS COMPUTER PROGRAM PACKAGE - (Reference: LACFD,LACRD,& OCEl'lA HYDRAULICS CRITERIOt\I:! *x r***+**I*~XIX********~*****~****t*****~********************************** (((((((i((((!(((((<((;((({((~(r({({<(({?~)):)):))))))jj)?;jjj:):)):)?j:);)))):)))?;j; (Cj Copyright 1982 Advarbced Engineering Software [AESI Especially prepared for: t4ANITOU ENGINEERING COWANY ({<(((ii(i<((((!<<((((<(({((((((((((~()?~):))))?~)?j):)}):)j)j:);)j:)??:?)?:):):)))?:~ **I****X**YX****+*+**********************~********************************** NOTE: STEADY FLOld HYDRAULIC HEAD-LOSS COMPUTATIONS mSED OF4 THE MOST CCNSERVATI'JE FORI.IULAE FROM ?HE CURRENT LACRD ,LACFCD I AND OCEMA DESI GY wtuALS, DOIJNSSPEAM PRESSLIRE PIPE FLOW CONTROL DATA: NODE NLIMEER = 31 0.10 PIPE DIAIIETERIINCH:) = 18.00 FLOINLINE ELEVATI ON = 258.85 PIPE FLCII.dICFS! = 9.40 ASSUIIEL'! DO!JKSTREAM CONTROL HGL = 262.66t ...................................... ...................................... ....................................... """~""""""""""""""""~""""""""""""-"""""- PRESSURE FLW PROCESS FRO!? NODE 31O.10 TO NODE 305.@0 IS CODE = 1 UPSTREAM NUDE 305 .00 ELE'WTION = 25C. 28 CALCLILATE PRESSURE FLO!I FRICTION LOSSESILACFCD): PIPE FL@!,! = 9-40 CFS PIPE DIAMETER = 18.00 INCHES PIPE LENGTH = 33.25 FEE? t.1Armn.m rd = .o1m SF=(O./K:!++2 = (I 9.40>/( 113,7?7jj**2 = .@U68233 HF=L*SF = I 33.25)*( .0068233:1 = .227 NODE 305.@U : HGL= < 262.893?;EGL= ( 263.332?;FL@WLINE= ( 259.280) ....................................... ....................................... PRESSURE FLOld PROCESS FROM NODE 305 .@@ TO NDE 305.10 IS CODE = 8 UPSTREAM NODE 305.10 - ELEVATION = 259.28 - ..................................... PIPE FLOI,,I(~.'S> = -4LCULATE PRESSURE FLOI:! CATCH BASIN ENTRANCE LOSSESILAC:FCW : 9.40 PIPE DIAMETER!INCH) = 18.0@ PRESSWE FLOI.J VELOCITY HEAD = ,437 ?~igPE 3@5.1@ : HGL= ( 26,3,4;Oj;EGL= CATCH BASIN Et4EEG''I LOSS = .2x(VEL@CJT'( HEAD; .2*I .439:1 = ,088 ( r )c:..,L~,.,lFi@WLINE= , c . .-, c, , . < 25?.280> ............................................................... ct.,., r,c ~C.CCC,,UC c, n,, ,li,? ....,.. ." "" ....................................... ...................................... PRESSEFE FLoi:.! PRilLEC? CROCI NODE 3085.10 TO tl'ODE 3075.Dt 15 COOE = 1 IJPST4EA:I 3;175 ~ E i E'.?kT I Of4 = 84, .Pd ....................................... ""_"""""""""""""""""""""""""""""""-"""" - PRESSUPE FLO:..d PROC.EE.5 FF'OY i.103E 3075 .C[I TO I4ObE 3075. 10 IS CODE = 5 'STREAt: tW!E 3075. 10 E LE?'AT I OYI = e ,!, . 8 i l- """"""""""""""-"""""""""""""""""""""""- ...................................... FRE:?SJF.E FLO:.:! PRZICESS FF.Or3 NODE ?C!6e. 10 TO IqC!DE AWL, PC! 13 CODE = 1 I_'?SSTHE&:I< !,:[$[)E ?c'72,(!0 EL El.)c\.T I [IN = v7. (19 ___r END OF PRESSURE FLOW H'(DR4LlLIC.S PIPE S'I'STEI' ...................................... ...................................... "~""""""""""""""""""""""""""""""""""""- EC'SLIPE FLCI!,.! PPOCESE; FPC':' k!C![)E 3C143.00 TC t.!O[!E 3[14?. 10 IC CODE = 8 IJPSTREA!.', N<l5E 3043. 1C ELEIvJ&TI@?4 = IlS,C[i ....................................... ....................................... ...................................... FRECSilFE FLO;j PF.!:t:,EC$ FP?'A, r.iU:mE 3045. 10 TO P:ODE 2030 .0C! IS CODE = 1 U.F'S?pE&!.; I.:!][lE 3<!>0 ,C[I ELE'.JATIU'\I = 135.7'; - &a/ L /wF &-/ ............................................................................ 9-26-86 PRESSURE PI PE-FLOW HYDRAULICS COMPUTER PROGRAM PACKAGE .- (Reference: LACFD,LACRD,B OCEtlA HYDRAULICS CRITERION! ............................................................................ <(((((((({(((<(({(((({{((((((({((({((())))))>)))))))))))))))))))?~))))?))))) (C) Copyright 1982 Advanced Engineering Software [AESI Especially prepared for: MANITOU ENGINEERING COblPANY ((((((((!{(((((({{((((<((((((((({{((<{?)?):)):);)))):))))~:)))~))))))?))))?))))))) ............................................................................ NOTE: STEADY FLOW H/DRAULIC HEAD-LOSS CRtlPUTATIOt4S EASED ON THE M@ST CONSERVATIVE FORMULAE FROH THE CURRENT LACRD,LACFCD, AND OCEMA DESIGN rmwLS. DOLINSTREAM PRESSURE PIPE FLOW CONTROL DATA: NODE NUNREF: = 125.00 PIPE DIAMETERIINCH) = 42.00 FLOIJLINE ELEVATION = 268.93 PIPE FLOI.d(CFS) = ASSUMED DOIJNSTREAII CONTROL H6L = 272.430 97 .70 ...................................... """"""""-"""""""""""""""""""""""""""""- """"""i"""_"""""""""""""""""""""""""""" ...................................... PRESSURE FLOW PROCESS FROM NODE 125.00 TO NODE 120 .00 IS CODE = 1 UPSTREAM NODE 120. 00 ELElfATl ON = 270.97 CALCULATE PRESSLIRE FLOW FRICTION LOSSESlLACFCD:! : PIPE FLON = PIPE LENGTH = 5'7.70 CFS 102.00 FEET PIPE DIAMETER = 42.00 INCHES SF=(Q.'K)ar2 = (I 97.70)./! 1089,?47)j**2 = .@OS0349 NODE 120.00 : HGL= < 273.250);EGL= < 274.851);FLOWLINE= ( 270.870) HF=L*SF = I 102.00!*( ,0080349) = ,820 PRESSURE FLOW ASSUMPTION USED TO ADJUST HGL AND EGL LOST PRESSURE HEAD USING SOFFIT CONTROL = NODE 120.00 : HGL= ( 274.470);EGL= < 276.071?;FLOlnlLINE= < 270.970> 1.22 rlArmIwS rd = ,01200 ...................................... ," " ..................................... " PRESSURE FLOlJ PROCESS FROM NODE 120 .00 TO NODE 119.00 IS CODE = 5 UPSTREAM NODE 119.00 ELEVATION = 270.97 ---------------""---"""""""""""""~"""""""""""""~ CALCULATE PRESSURE FLOM JurrrIord LOESEC: NO. DISCHARGE DIAMETER AREA VELOCIT'I DELTA H!I n 7 - .^ r - . ._ .. .~~ ~ ~~ ...................................... ...................................... PRESSURE FLOW PROCESS FROM NODE 120 .00 TO NODE 119 -00 IS CODE = 5 UPSTREAM NODE 1 19.00 ELEVATIOI.1 = 270 -97 CALCLILATE PRESSURE FLOIJ JUNCTION LOSSE?,: -. DISCHARGE DIAMETER AREA VELOCITY DELTA H!? 87.7 42.00 9.621 9.115 90 .000 1 ,290 i 9,7.7-- - {~,$p---- S=*mTix55 " " 3 10.0 18.00 1.767 5,459 4 0.0 47.500 0 .00 0 .000 0.000 5 0 .000 0 .0===R5 ERUALS BASIN INPUT=== " " - - LACFCD AND OCEMA PRESSURE FLOld JUNCTION FORMULAE USED: DY=IR2*U2-Ql*Vl*COS(DELTAl)-Q3*!13*COS(DELTA3)- Q4*Y4*COS!DELTA4))/!(Al+A2~*14.1j UPSTREAM MANNINGS N = .01200 DOWNSTREAM MANNINGS N = .@1200 UPSTREAM FRICTION SLOPE = ,00447 DOIJNSTREAM FRICTION SLOPE = ,00803 JUtJCTION LENGTHCFEET) = 4.00 FRICTION LOSS = ENTRANCE LOSSES = 0.000 ,029 JUNCTION LOSSES = DY+HUl-H112+~FRICTION LOSS)+!ENTRANCE LOSSES:) NODE 119.00 : HGL= < 277.578>;EGL= < 278.868>;FLOWLINE= < 270.?70> JUNCTION LOSSES = 3.079t 1.290- 1,4@1t( .029>+1 0.00@) = 2.797 AVERAGED FRICTION SLOPE Ir4 LwrmlnN ASSUMED AS ,00725 ...................................... ~"""""""""_"""""""""""""""""""""""""""" PRESSURE FLO1.d PROCESS FROM NODE 119.00 TO NOOE 117.00 IS CODE = 1 UPSTREAM NODE 117.@0 ELEllATION = 287.92 " .................................... CF~LCULATE PRESSURE FLOW FRI CTI ON LOSSES( LACFCD) : PIPE LENGTH = PIPE FLON = 87.50 CFS 66.46. FEET PIPE DIAMETER = 42.00 INCHES SF=IQ./K)*+2 = I( HF=LrSF = ( 44.46!*(! .0064447) = 87.5@:)/( 1087.947)!**2 = ,0064447 .428 MANrJIrw N = ,01200 NODE 117.00 : HGL= i 278.012i;EGL= < 279.297);FLOWLlNE= < 287.020) PRESSURE FLOW ASSUMPTION USED TO ADJUST HGL Arm EGL LOST PRESSURE HEAD uslm SOFFIT COrmoL = ....................................... NODE 117.00 : HGL= < 291.420>;EGL= < 292.704);FLOWLINE= < 287.920) 13.41 ............................................................................ PRESSURE FLOI.4 PROCESS FROM NODE 117.00 TO NODE 11 4 .00 IS CODE = 5 UPSTREAM NODE 1 1 6.00 ELEVATI ON = 287.92 CALCULATE PRESSURE FLOIJ JUNCTION LOSSES: ...................................... NO. DISCHARGE DIAMETER AREA VELOCITY DELTA HV 1 85.5 42.00 2 87.7 9.421 42.00 8.887 0 .OD0 1.226 9.421 9.115 " 1 .290 3 0.0 0 .00 0 ,000 0 .000 a .ooo 4 0 .0 0 -00 0 .ROO 5 2.2===R5 EQUALS BASIN INPUT=== 0 .000 0 .000 - - ""FCD AND OCEMA PRESSURE FLOW JUNCTION FORMULAE USED: -lR2*1J2-Ql*V1+COSIDELTAl)-Q3*'~~3*COS~DELTA3:)- Q~*V~+COSCDELTA~~)~/(~A~+A~~~~~,~:I UPSTREAM MANNINGS N = .01200 UPSTREAM FRICTION SLOPE = ,00615 nnl.lb,tCTwmt.d cG1r-rlnb.l CI nvc = nn1.47 DClldI4STREAM IIANNINGS 14 = ,0 1 200 UPSTREAM MANNINGS N = .0120@ DCl!JIJSTREAM PlAFJNIrJGS N = .0 1200 UPSTREAM FRICTION SLOPE = .Oil615 AVERAGED FRICTION SLOPE IN JUIJCTIOi4 ASSUMED AS .00631 DOWNSTREAM FRICTION SLOPE = .@I3647 JLINCTION LENGTH(FEET) = 4.00 FRICTION LOSS = ,025 7 ENTRANCE LOSSES = .258 WHOLE LOSSES GREATER THAN THOMPSON MOMENTUM LOSSES I.IOMENTUM LOSSES = 064 MArJHOLE LOSSES = ,065 JUNCTION LOSSES = DYtH1J1-HU2t(FRICTION LOSS:l+iENTRANCE LOSSES) JUNCTION LOSSES = NODE 116.00 : HGL= i 291.826);EGL= < 293.052);FLOWLINE= < 287.920) ,128.t 1.226- 1.290t': .02S)+( ,258) = ,348 " "_ " " - "_""" _II" """"-"""""_"""""""""""""""""""""""""""" ....................................... PRESSURE FLOld PROCESS FRC1i-l NODE 11 6.00 TO NODE 115.00 IS CODE = 1 UPSTREAM NODE 11 5.00 ELEVATION = ~12.18 CALCLILATE PRESSLIRE FLOW FRICTION LOSSESiLACFCD) : PIPE FLOW = 85.50 CFS PIPE LENGTH = 64.00 FEET PIPE DIAMETER = 42.@0 INCHES SF=<Q/K)**2 = (( P5.5@!/( 1089.947:))**2 = .GO61535 HF=L*SF = < 64.@0)*( ,00615351 = NODE 115.00 : HGL= < 292.220>;EGL= i 293.446);FLOWLINE= < 312.180) .3?4 rlANr.dImS rd = .DIZCICI """""""""""""""""""""""~""""""""""""""- PRESSURE FLOIJ ASSuwTIor4 llSEci TO ADJUST HGL Aw EGL LOST PRESSURE HEAD USING SOFFIT CONTROL = 23.46 NODE 115.00 : HGL= i 315.680i;EGL= < 316.906:);FLOWLINE= i 312.180:) ...................................... PRESSLIRE FLOW PROCESS FROM NODE 115.00 TO NODE 114.OO IS CODE = 5 "STREAM NODE 1 14. @0 ELEVATION = 312.18 CALCULATE PRESSURE FLOW JUNCTION LOSSES: - ..................................... NO. DISCHARGE DIAMETER AREA VELOCITY DELTA 1 HIJ 85.5 42.00 8.621 8.887 6.500 1 * 226 2 85.5 42.00 5.621 8.887 " 3 0.0 0 .OO 0 ,000 0 .00@ 0 .000 1.226 4 0 . 0 0 -00 0.000 0 .000 0.000 c' 0 .0===05 EQUALS BASIN INPUT=== - r - I LAC:FCD AND OCEMA PRESSURE FLOW JLINCTION FORHULAE USED: DY=102xV2-~l*Vl*COSIDELT~l~-~3~1J3xCOS':DELTA3)- Q4~V4*COS~DELTk4~:)/1~~1tA2~*16.11 UPSTREAM MANNINGS N = .@12@C1 UPSTREAV FRICTION SLOPE = .00615 AVERAGED FRICTION SLOPE IN JUNCTION ASSUMED AS .00615 DO1.JNSTREAI-I FRICTION SLOPE = ,00615 ENTRANCE LOSSES = 0.000 JUNCTION LENGTH(FEET1 = 4.00 FRICTION LOSS = .02S MANHOLE LOSSES GREATER THAN THOMPSON MOMENTUM LOSSES MANHOLE LOSSES = .Ob1 DOIANSTREAM w+rJtdImS N = ,01200 MOMENTUM LOSSES = ,016 JUNCTION LOSSES = DYtHUl-H?12+<FRICTION LOSS!tIENTRANCE LOSSES) JUNCTION LOSSES = .016+ 1.226- 1.22tt< .025)+( 0.000) = ,086 NQ@E 114.00 : HGL= < 315.766>;EGL= < 316,992:~;FLOI.;ILIr.IE= ( 312 180) I ....................................... PRESSLIRE FLOW PROCESS FRO3 IJODE 114.00 TO NOUE 110 .00 IS CODE = 1 UPSTREfXI NODE 110 ,@0 ELE?JATIUN = 312.97 rnl rill ATE GGCCCIIGK CI nt.1 rD'lrTin1.l I ncccc/t nrcrr:, ""-""""~""""""""""""""""""""""""""""~""~ ...................................... ...................................... PRESSURE FLOW PROCESS FROM NODE 114.00 TO NODE 110 .00 IS CODE = 1 UPSTREAM NODE 1 10,OO ELEVATION = 312.97 CALCULciTE PRESSURE FLOlJ FRICTION LOSSES(LACFCD): ....................................... ,L P E F L OIJ = 85.50 CFS ('E LENGTH = 112.66 FEET PIPE DIAMETER = 42.00 INCHES SF=(Q/K)**2 = <( rlarwIrm r4 = .01200 HF=L*SF = < 112.68!*( .006.1535:) = * 693 NODE 110.00 : HGL= < 316.459);EGL= < 317.686);FLOWLINE= < 312.970) PRESSLIRE FLOL! ASSUtIPTION USED TO ADJUST HGL AND EGL LOST PRESSURE HEAD USING SOFFIT CONTROL = NODE 110.00 : HGL= < 316,47CO;EGL= < 317.696>;FLOWLINE= < 312.970) .01 85.50)./r 1089.?47j)**2 = .0061535 ...................................... """-""""""""""""""""""""""""""""""""""~ ...................................... PRESSURE FLOlJ PROCESS FROPI NODE 110.00 TO NODE 109.00 IS CODE = 5 UPSTREAM NODE 108.00 ELEVAT I ON = 31 2. 97 -"""x"""""- """"_ "-"""="-.~_ "" """"""""""_ - CALCULATE PRESSURE FLOW JUNCTION LOSSES: NO. DISCHARGE UIAMETER AREA VELOCITY DELTA H'J 1 77.5 42.00 9.621 8.055 0 .000 2 1 .OD8 85.5 3 42.00 9.621 0.0 0.00 0 ,000 - 8.887 0.000 1 ,226 0.000 4 0 .0 0 .00 0 .000 0.000 0.000 5 8.0===Q5 EQUALS BASIN INPUT=== " - LACFCD AND OCEMA PRESSURE FLOW JllNCTION FORMULAE USED: - Q~*Y~*CCISIDELTA~:!)/!(A~+A~)+~~.~) UPSTREAM MAI4NINGS t.l = .01200 DOWNSTREAM MANNINGS N = ,0 120 0 UPSTREAM FRICTION SLOPE = .0050b DOWNSTREAM FRICTION SLOPE = ,00615 AVERAGE@ FRICTION SLOPE It4 JUNCTION ASSUMED AS ,00560 JUNCTION LENGTH(FEET) = 4.00 ENTRANCE LOSSES = ,245 FRlCTlDN LOSS = .022 DY=(Q2xi..~2-Q1*Vl+COSIDELTAi)-Q~*~~3*COS(DELTA~)- JUNCTION LOSSES = DYtHUl-HV2tlFRICTION LOSSj+IENTRANCE LOSSES:) JUNCTIOP! LOSSES = .437+ 1.00E- 1.226t( ,022:)tI .245) .486 NODE 109.00 : HGL= < 317.175);EGL= < 31&.183i;FLOl\'LII4E= < 312.970:) ............................................................................. PRESSURE FLOW PROC:ESS FROM NODE 109.00 TO NODE 105.00 1s CODE = 1 UPSTREAM NODE 105.00 ELEWTION = 313.97 CALCULATE PRESSURE FLOlnl FRICTION LOSSESILACFCD j : PIPE FLOW = 77.50 CFS PIPE DIAMETER = 42.00 INCHES PIPE LENGTH = SF=(Q./K:)*rZ = <I 52.78 FEET MANNJNGS N = .01200 HF=L*SF = I 77.50)/( 1089.947))**2 = .0050558 52.78)*! .0050558) = .267 NODE 105.00 : HGL= < 317.442j;EGL= < 318,45@);FLOWLINE= < 313.970) PRESSURE FLOW ASSUMPTI014 USED TO ADJUST HGL AND EGL -ST PRESSURE HEAD USING SOFFIT CONTROL = .03 ...................................... ...................................... I -.3E 105.00 : HGL= < 317.470);EGL= < 318.478~;FLOWLINE= < 313.970) ....................................... """"_"""""""""""""""""""""""""""""""""~ PRESSLIRE FLCM PRClC.ES5 FROM NODE lCl5.00 TO NODE l(14.0ti IS CODE = 5 UPSTREkrl NODE 104.00 ELEV&TIOIJ = 313.97 """ " ""_ " ................................... PRESSLIRE FLOIJ PROC.ESS FROM NODE 105.00 TO NODE 104.00 IS CODE = 5 UPSTREAM NODE 104.00 ELEVATION = 313.87 """""""""""""""""""""""""""""- ....................................... CALCULATE PRESSURE FLOW JLNCTION LOSSES: NO. DISCHARGE DIAMETER AREA VELOCITY DELTA HV 1 77.5 36.00 7.069 10.964 29.800 1 .P67 - 77.5 42.00 3 9.621 0 .0 0 .00 0 .on0 0 .000 8.055 1.008 4 0.000 0.0 0 .on 0.000 0.000 0 .000 5 0 .o===Qs EQUALS BASIN Iwus=== - 7 " - - LACFCD AND OCEIlA PRESSURE FLOW JUNCT1M.I FORMLILAE USED: DY=I02*~~2-Ql~Vl*COSIDELTAl~-Q3*U3*COSIDELTA3~- ~~*V~*COSIDELTA~:I),/!~A~*A~~*~~.~) UPSTREAM MANNINGS N = ,01200 DMJNSTREAFI MANNINGS N = .012?0 UPSTREAV FRICTION SLOPE = .01150 AVERAGED FRICTION SLOPE IN JUNCTION ASSUMED AS .00828 DOWNSTREAM FRICTION SLOPE = .00506 JUNCTION LENGTHlFEET) = 4.00 FRICTION LOSS = .033 ENTRANCE LOSSES = 0 ,000 JLNCTION LOSSES = DYtHUl-HU2+(FRICTION LOSS)+IENTRANCE LOSSES:] JUNCTION LOSSES = -.421+ 1.667- 1.008+( .033!+( 0.000! = .471 ~iu+.ui.r#~-\~~fi~~~~t-4~~~~.r:L~L~t~ "-"" """"""_"""""""""""""""""""""""""""""""~ PRESSURE FLW PROCESS FROM NODE 104.00 TO rdo[)E 1047.00 IS CODE = 1 UPSTREP NODE 1047.00 ELEVATION = 316.51 ."-CULATE PRESSURE FLOW FRICTION LOSSESlLACFCD:! : PIPE LENGTH = 1 d? -51 FEET MAMJINGS N = .01200 HF=L*SF = I SF=IU./Kj*r2 = (I 77.50)./( 722.568):)**2 = ,011503~ 169.51:)*( ,0115039) = 1 .?SO NODE 1047.00 : HGL= ( 318.03Zi;EGL= < 320,8?Y:!;FLOWLINE= < 316.510) ...................................... .'E FLOIJ = 77.50 CFS PIPE DIAMETER = 36.00 INCHES ...................................... PRESSURE FLOIJ ASSUMPTION USED TO ADJUST HGL EGL LOST PRESSLIRE HEAD USING SOFFIT CONTROL = -48 NODE 1047.00 : HGL= < 31?.510>;EGL= < 321.377:;;FLOWLINE= i 316.510) ============================================================================ PRESSURE FLOW PROCESS FROM NODE 1047.00 TO NODE 1046.00 IS (:ODE = 5 UPSTREAM NODE 1046.00 ELEVATION = 316.51 CALCULATE PRESSURE FLOIM JUNCTION LOSSES: ....................................... NO. DISCHARGE DIAMETER AREA VELOCITY DELTA 1 HV 68.6 30 .00 4.909 13.975 63.300 2 77.5 36.00 7.069 10.964 3.033 3 8 .? 18.00 1 ,767 5.036 1 I 867 4 0 .000 0 .[I 0 .00 0 .@00 0 ,000 0 .no0 5 0.0===05 EQUALS BASIN INPUT=== " - - LACFCD AND OCEMA PRESSURE FLOW JUNCTION FDRIIULAE USED: DY~lQ2*V2-Q1*U1*C@S(DEL?Al)-03*V3*COS!DELTA3i- 04*V4*COSiDELSA4:))/lIAl+A2)*16.1? UPSTREAM MANNINGS N = .Dl200 UPSTREAII FRICTIOI.1 SLOPE = .E2383 DOWNSTREAI1 FR!CTIOII SLOPE = ,01150 DOI,WTREAM tw,rmIrm N = .OI 200 AVERAGED FRICTION SLOPE It4 JLIWTION ASSLIMED A:. .rtt~x? LIPSTREA'I MANNINGS N = ,01200 UPSTREAI4 FRICTION SLOPE = .02383 DOl.dNSTREAM MANNINGS N = ,01200 AVERAGED FRICTION SLOPE It4 JUt4CTION ASSUMED AS ,01767 DOWSTREAPl FRICTION SLOPE = .01150 - JIINCTION LENGTH!FEET) = 4.00 FRICTION LOSS = ,071 wdNCT1OF.l LOSSES = DYtHVl-H'J2~!FRICTIUN LOSS)+(ENTRANCE LOSSES, NODE 1046.00 : HGL= < 321.521);EGL= ( 324.554!;FLOl.~LINE= < 316.510, JUNCTlOt4 LOSSES = 1.940t 3.033- 1.867+! .071)ti 0,000) = 3.177 TRANCE LOSSES = 0.000 ....................................... ....................................... PRESSURE FLOlnl PROCESS FROFl NODE 1046.00 TO NODE 1049.00 IS CODE = 1 UPSTREAM NODE 104S.00 ELEVATION = 321.47 CALCULATE PRESSLIRE FL0I.J FRICTIOi.4 LOSSESCLACFCD:]: PIPE FLOW = PIPE LENGTH = 68.60 CFS 115.36 FEET PIPE DIAMETER = 30.00 INCHES MANNINGS N = .Dl200 HF=L*SF = < 115.36)*1 .0238339:1 = 2.749 NODE 1049.00 : HGL= { 324.270>;EGL= < 327.303?;FLWLINE= < 321.470) SF=<Q/Ki+*2 = (( &.60j/! 444.352!)**2 = ,023833S ...................................... UPSTREAM NODE 1048.00 ELEVATION = 321.47 PRESSURE FLOU PROCESS FROM NODE 1049.00 TO NODE 1048.00 IS CODE = 5 ....................................... CALCULATE PRESSURE FLOId JU!.ICTIOtJ LOSSES: NO. DISCHARGE DIAMETER AREA VELOCITY DELTA HV 1 62.0 30.10 4.909 12.631 55.400 2.477 -"+---? ,n lo. 0 , -. ~"-"-~~"tfu~"-"-"""~ -, """"" I .. 6.t 18.00 4 1.767 0 . 0 3.735 10 .OD@ - 0 .00 0 .eon 0.000 0 .000 5 0 .@===B5 EQUALS BASIN INPUT=== ", c - LACFCD AND OCEMA PRESSURE FLOW JUNCTION FORMULAE USED: DY=1Q2r1~2-~l+V1~COSIDELTAl:)-a3+V3rCDS!DELTA3~- ~4~~~4*COSlDELTA4~~/~~Al+A2~*16.1~ UPSTREAM MANNINES 14 = .01200 DObJNSTREAM MAE4blIIIFJGS N = .01200 UPSTREAM FRICTION SLOPE = ,01947 AVERAGED FRICTION SLOPE IN JUNCTIOI4 ASSLIMED AS ,02165 DOWNSTREAM FRICTION SLOPE = .I22383 JUNCTION LENGTHIFEET) = 4.00 FRICTION LOSS = ,087 ENTRANCE LOSSES = 0.000 JUNC.TICt4 LOSSES = DYtHVl-HV2t~FRICTION LOSS)t!Et.ITRANCE LOSSES) JUNCTIOW LOSSES = 3,098t 2.477- 3.033+( .O87:lt( 0.000i = 2.630 NODE 1048.00 : HGL= .I 327.455i;EGL= < 329,Y33i;FLUWLINE= < 321.470) """""""""_"""""""""""""""""""""""""""~~~ PRESSURE FLOW PROCESS FROM NODE 1048.00 TO NODE 840.00 IS CODE = 1 UPSTREAM NODE 840.00 ELEVATION = 328,64 CBLCULATE PRESSURE FLOW FRICTION LOSSES!LACFCD): E FLClld = PIPE LENGTH = 62 -00 C.FS PIPE DIAMETER = 30.00 INCHES 147.00 FEET MAWINGS N = .01200 SF=IR./K)s+2 = (I 62.cIo:J./! 444.352):1**2 = ,0394683 HF=L*SF = I NODE 840.00 : HFL= 330,317>;EGL= < 332,794?;FLOWLI~.IE= ( 328.640) 147.00)*! .@194684::' = 2.862 PRESSLIRE FLCIIJ ASSIJNPTION ILISED T@ ADJUST HFL AI.I[! EGL ...................................... -------""~"""""""""""~""""~""""""~"~~~""""""" . "._ ^"" ~ ...................................... LOST PRESSURE HEAD USING SOFFIT CONTROL = PRESSURE FLOlJ ASSLIMPTION LISED TO ADJLIST HFL AND EGL i82 NODE 840.00 : HGL= < 331.140?;EGL= < 333,61??;FLOGlLINE= < 328.640) ...................................... " ...................................... UPSTREAM NODE 839.00 ELEUATION = 328.64 CALCULATE PRESSURE FLOW JUNCTION LOSSES: ISSURE FLOW PROCESS FROM NODE 840.00 TO NODE 839.00 15 CODE = 5 """""""""_"""""""""""~""""""""""""""""" NO. DISCHARGE DIAMETER AREA VELOCITY DELTA H!? 2 1 62.0 30 .0@ 4.909 12.631 0 .000 2.477 62.0 3 30 .@O 4.009 12.631 " 2.477 4 0 -0 0 .00 0 ,000 0 .000 0 ,000 0 -0 0 .00 0 .000 0 .005 0 .oil0 J o ,O===Q~ EQUALS BASIN INPUT=== - c - LACFCD AN5 OCEMA PRESSURE FLOI.:! JUNCTION FORMULAE USED: DY~~Q2~V2-Ql+Ul*COS~DELTAl~-R3*U3~COSIDELTA3~- Q4*~~4*C@S~DELTA4~~/~~Al+A2~*16.l~ LIPSTREAM MANNINGS N = .@1200 UPSTREAM FRICTION SLOPE = ,01947 DOldbISTREAM FRICTION SLOPE = .0104? AUERAGED FRICTION SLOPE IN JUNCTION ASSLPIED AS ,01947 JUNCTION LENGTHIFEET) = 4.00 FRICTION LOSS = ,078 EI4TRANCE LOSSES = 0.000 MANHOLE LOSSES GREATER THAN THOMPSON MOMENTLlM LOSSES MOMENTUM LOSSES = -.@@!I MANHOLE LOSSES = .124 JUNCTION LOSSES = DY+Hi~~1-HV2tIFRICTION LOSS)tIENTRANCE LOSSES) DOlnlNSTREAM MANNINGS N = ,01200 - ICTION LOSSES = -.000+ 2.477- 2.477tI .078)t! 0.000) = .202 b.dL'E 839.00 : HGL= < 331.342);EGL= < 333.810);FLOl;ILINE= < 328.44Ui ...................................... ...................................... PRESSURE FLOld PROCESS FROM NODE 839.00 TO NODE 835.00 IS CODE = 3 UPSTREAY NODE 835.00 ELEVATION = 349.75 CALCULATE PRESSURE FLOW PIPE-BEND LOSSESIOCEMA) : PIPE FLDW = 62.00 CFS PIPE LENGTH = PIPE DIAMETER = 30.00 INCHES 270.70 FEET MANNINGS N = .01200 CENTRAL ANGLE = 14,600 DEGREES PRESSURE FLOW AREA = 4.909 SQUARE FEET 'JELOCIT'I HEAD = 2.477 FLOlA ?IELOCITY = 12.63 FEET PER SECOND HE=KHa(VELDCITY HEAD) = I .101j*I 2.477:) = ,249 BEND COEFFICIENT(KB) = ,1007 PIPE C.O!.I'JEYANCE FACTOF. = FRICTION LOSSES = LrSF = I 444.352 270.70)*i ,0194684) = 5.270 FRICTION SLOPEtSF) = ,0194684 NODE 835.00 : HGL= < 336.861j;E6L= < 339.338?;FLOWLINE= < 349.750) PRESSURE FLDW ASSUMPTION USED TO ADJUST HGL AND EGL LOST PRESSURE HEAD USING SOFFIT CONTROL = 15.39 NODE 835.00 : HGL= < 352.250>;EGL= < 354.727>;FLOWLINE= < 349.750:) """""""""_"""""""""""""""""""~"""""""" "i"====""""""_"- " """"""""""""""""""""""""- ----------------==~""""""""""""""""~"""""""~~ ISSURE FLO!J PROCESS FROM NODE 835 -00 TO NODE 834 -00 IS CODE = 5 UPSTREAM NOOE 834.00 ELEUATION = 349.7; ...................................... CALCULATE FRESSLIRE FL0I:J JLINCT1DP.l LOSSES: NO. DISCHARGE DIAtlETER AREA VELOCITY DELTA H!, 1 c,2.0 3 0 , 0 0 4.309 12.6.31 CI . o 0 o 2.477 2 62.0 30.00 4.909 1?.C,31 " 3.477 CALCLILATE PRESSURE FLOIM JUNCTION LOSSES: N@. DISCHARGE DIAtlETER AREA VELOCITY DELTA HV 1 62.0 30.00 4.909 12.631 0.000 2.477 2 62.0 30 .00 4.909 12.631 " 2,477 3 0 .0 0 .00 0 .000 0.000 0 .@00 - -1 0.0===Q5 EQUALS BASIN INPUT=== -4 0.0 0 .00 0 .00@ 0.000 0 .000 c - LACFCD AND OCEMA PRESSURE FLOld JUNCTION FORMULAE USED: DY=IR2*'J2-Rl*VlICOS([!ELTAl:!-~3*'~'3*COS!DELTA3~- ~4*'J4*COS!DELTA4:)j./!IA1+A2)+16,1) UPSTREAM MANNINGS N = ,01200 DOWNSTREAM MANNINGS N = ,01200 UPSTREAM FRICTION SLOPE = .01947 AVERAGED FRICTION SLOPE IN JLFJCTION ASSLIMED AS ,01947 DOWF4STREAM FRICTION SLOPE = .01?47 JUNCTION LENGTHCFEET! = 4.00 FRICTION LOSS = .078 ENTRANCE LOSSES = 0.000 MANHOLE LOSSES GREATER THAN THOYPSON MOMENSLIM LOSSES MOMENTUM LOSSES = -.@DO MANHOLE LOSSES = .124 JUNCTION LOSSES = DYtHV1-HVZtiFRICTION LOSS)t!ENTRANCE LOSSES) NODE 634.00 : HGL= < 352.452i;EGL= < 354.929?;FLOWLINE= < 339.750: JUEJCTIO1.1 LOSSES = -.000t 2.477- 2.477t! .07E!t1 0.0@0.l = .202 ........................................................................ PRESSLIRE FLOd PROCESS FROM NODE 834.00 TO NODE 830.00 IS CODE = 3 LIPSTREAM NODE 830 .OO ELEIJATI ON = 352.67 ....................................... - CALCULATE PRESSURE FLOW PIPE-BEND LOSSESCOCEMA) : "E FLOW = 62.00 CFS PIPE DIAflETER = 30.00 INCHES . .+E LENGTH = 133.94 FEET MAW IN&S N = .0120@ CENTRAL ANGLE = 38 ,600 DEGREES PRESSLIRE FLOW AREA = 4.909 SQUARE FEET VELOCITY HEAD = 2.477 HR=KB*IVELOCITY HEAD) = I .164)+< 2.4771 = .40C. PIPE CPN'JEU'ANCE FACTOR = 444.352 FRICTI0f.I SLOPEISF:) = .@I94684 FRICTION LOSSES = LISF = ! 138.94)*! .01?4684) = 2.705 FLON VELOCITY = 12.63 FEET PER SECOND BEFU'D COEFFICIENTIKB) = ,1637 "t~~"a~grrr#~=-~-355;5~r;~~t"f-~~rf;P:r;~~mi~it;=-t-~cr~~,"-""""""- ." , -"""""""""_""""""""""""""~"""""""""""""~ -"""""""""""""""""""""""""""""""""""""- UPSTREAM NODE 829.00 PRESSllRE FLOW PROCESS FROM NODE 830 -00 TO NODE E29.00 IS CODE = 5 CALCULATE PRESSURE FLOM JUNCTION LOSSES: ELE'JATI ON = 352.61 ....................................... NO. DISCHARGE DIAMETER 1 dd.7 2 30 .OO 62.0 30 .00 3 4 6.3 18.00 5 0 .@ 0 .00 0. @===a5 EQUALS LACFCD AND OCEMA PRESSURE ec AREA VELOCITY DELTA H'J 4.909 11.347 51 .200 1-99? 4.909 12.631 " 2.477 1.767 3.565 90 .000 0 .DO@ 0 .000 0.000 - BASIN INPUT=== FLOLJ JUNCTION FORMULAE USED: - UPSTREAM NODE 782.00 PRESSIURE FLOW PROCESS FROM NODE e?? .OO TO NODE 782 .00 IS CODE = 1 ELEVATION = 353.34 ...................................... CALCULATE PRESSURE FLOW FRICT1OI.I LOSSES(LACFCD1: PIPE LENGTH = PIPE FLOLJ = 55.70 CFS PIPE DIAMETER = 3@.@0 INCHES 66.88 FEET SF=(Q/K;)**2 = 11 HF=L*SF = ( 66.88)*( .0157129:) = NODE 782.00 : HGL= < 359.132>;EGL= < 361.132);FLOWLINE= < 353.340) 1.051 MAN!~INGS rd = ,01200 55.70)./( 444.352))**2 = .0157129 PRESSURE FLOI.41 PROCESS FROM NODE 782.00 TO NODE 781 .00 IS CODE = 5 UPSTREAM NODE 761 .00 ELEVATION = 353.34 CALCULATE PRESSURE FLOW JUNCTION LOSSES: ...................................... NO. DISCHARGE DIAMETER AREA VELOCITY DELTA i 55.7 30 .OO 4.909 11,347 34.300 1 .999 H!, " 2 55.7 30 .oo 4.909 11.347 " 3 0.0 0 .000 0 .000 1 , 999 0 .on 4 0 .000 0.0 0 .no 0 .000 0.000 0 .000 - 5 0.0===65 EQUALS BASIN INPUT=== - LACFCL) AND OCEMA PRESSURE FLOW JUNCTION FORMULAE USED: DY=(GI2+V2-Ql*V1+COSiDELTA1~-Q3*'~J3*COS~DELTA3~- Q4*V4*COS(DELTA4~~.~~!!AltA2~rl6.1:~ ...................................... PRESSURE FLOW PROCESS FROM NODE 781 .@0 TO NODE 760 .00 IS CODE = 1 UPSTREAPI NODE 760 -00 ELEVATION = 370.19 CALCULATE PRESSURE FLOlnl FRICT1OI.I LOSSES1LACFCD): I .iE LENGTH = 144.00 FEET MAF4NIE.IGS N = .01200 HF=L*SF = ! SF=<GI./Kj**2 = !! 144.00)*( ,0157129:) = 55.70:1/1 444.352:))**2 = ,0157129 2.263 NDDE 7LC1.00 : HGL= { 3L2,153>;EGL= < 364.152j;FLOlJL1NE= { 370,190) PRESSURE FLCIld ASE.lUMPTION USE5 TO ADJIJST HGL AND EGL 'E FLOW = 55.70 CFS PIPE DIAMETER = 30.00 INCHES ....................................... I nrT onrrr,,nr Ilrhr~ ,,,71*,? mnrr7-r r.n/ITr,r.l ~~~ .<. =" PRESSURE FLOW ASSUMPTION USED TO ADJUST HGL AND EGL LOST PRESSURE HEAD USING SOFFIT CONTROL = 10.54 NODE 760.00 : HGL= < 372.690);EGL= < 374.68?:);FLOlJLINE= < 370,190> ...................................... "?SSLIRE FLOIJ PROCESS FROM NODE 760 .00 TO NODE 759.00 IS CODE = 5 jTREAM NODE 759.00 ELEVATION = 370.19 CALCULATE PRESSURE FLOW JUNCTION LOSSES: NO. DISCHARGE DIAMETER AREA VELOCITY DELTA HV 1 30.6 24.00 3.142 9.740 45.000 1 ,473 2 55.7 30 .00 4.907 11.347 " 1.999 3 4 25.1 0 .0 24 .00 3.142 7.990 45.000 0 .oo 0.000 0 .000 0 .ooo - 5 O.@===Q5 EQUALS BASIN INPUT=== - LACFCD AND OCEMA PRESSURE FLOW JUNCTION FORMULAE USED: DY=(Q2*V?-Ql~Vl*COS(DELTAl~-Q3*V3*COS(DELT~3)- Q4*V4*COS(DELTA4j)/(ifiltA2>*16.1~ UPSTREAM MANNINGS N = ,01200 UPSTREAM FRICTION SLOPE = ,51559 AVERAGED FRICTION SLOPE IN JUNCTION ASSUMED AS .015t5 DOWNSTREAM FRICTION SLOPE = .01571 ENTRANCE LOSSES = 0.000 JUNCTION LOSSES = DYtH'Jl-HV2t(FRICTIOE.l LOSSftiENTRANCE LOSSES) \ JUNCTION LOSSES = 2.156t 1.473- 1.999t( .063!+( 0.000! = 1.693 DOWNSTREAM MANNINGS N = .Dl200 JUNCTION LENGTHIFEET) = 4.00 FRICTION LOSS = .063 NO5E 759.00 : HGL= < 374.?@?i;EGL= < 376,38Z:);FLOIJLINE= < 370.19Oi 7 ". ........................ PRESSURE FLOW PROCESS FROM NODE 759.00 TO NODE 730.00 IS CODE = 1 UPSTREAM NODE 730 .00 ELEVATION = 374.23 ...................................... CALCULATE PRESSURE FLOIJ FRICTION LOSSESCLACFCD): PIPE FLOl.4 = 30.60 CFS PIPE LENGTH = PIPE DIAMETER = 24.00 INCHES 36.77 FEET rmmm N = ,01200 SF=IWK)**2 = (C 30.60)./( 245.076))**2 = .0155899 HF=L+SF = ( 36.77)*( .0155899! = NODE 730.00 : HGL= < 375.482>;EGL= < 376.955>;FLOWLIt.IE= < 374.230) .573 PRESSURE FLOW ASSUMPTION USED TO ADJUST HGL AND EGL LOST PRESSURE HEAD USING SOFFIT CONTROL = ,75 NODE 730.00 : HGL= < 37&.23@>;EGL= < 377,703:>;FLOWLINE= { 374.230) "---FiFtEWRE7RW+WEE%+*@* P " mmmc-~= 5"""- -. .................................................................... UPSTREAM NODE 729, @0 ELEVATION = 374.23 CALCULATE PRESSURE FLOW JUNCTION LOSSES: d ""-"""~"""_""""""""~"""""""""""""""""""" NO. DISCHARGE DIAMETER AREA VELOCITY DELTA 1 HV 14.7 18.00 1.767 9.450 45.000 1 .387 2 30.6 24.00 3.142 7.740 "7 13.9 18.00 1 ,767 7.866 45.000 1 .473 4 0 .0 0 .on 0 .000 0 .GOO 0 .a00 5 0 .0===Q5 EOUALS BOSIN INPUT=== " - - LACFCD AND OCEElk PRESSURE FLDIW JUNCTI ON FORMLlLAE USED: DY=!Q2*'~~2-ff1*i~~l*COS~DELT~l:l-Q3~'J3~COSi@ELTA~~~- Q~*V~*COS~@ELTA~):I./~~~~~A~~~~~,,~:~ I ~LC~JYRL ~LLW TRL~LC~.~, rnul'i luuut /~ll.l\U 111 i<l!LJt ~ ~L~;IT~"~~XLJC = J UPSTREAM NODE 72?. 00 ELEVATION = 374.2? CALCULATE PRESSURE FLOW JUNCTI ON LOSSES: ""_"""""""""""""""""""""""""""""""""""~ NO. DISCHARGE DIAMETER AREA VELOCITY DELTA H'J 1 16.7 18.00 i ,767 P .450 45.000 1 .387 2 30.6 24.00 3.142 9.740 " 1.473 3 13.9 18.00 1.767 7.866 45.000 - 4 5 0 .0 0 .00 0 .00@ 0 .@00 0.000 - 0 .0===05 EQUALS BASIN INPUT=== .- LACFCD AND OCEIIA PRESSLIRE FLOW JUNCTION FORMULAE USED: OY=(02r'J2-0l+Vl*COS(DELTAl)-Q3~U3*COSi~DELTA3~- UPSTREAM MANNINGS N = .01200 C!OIdWTREAM MANNINGS N = .0120@ UPSTREAP4 FRICTION SLOPE = .02154 DOWNSTREAM FRICTION SLOPE = ,01559 AVERAGED FRICTION SLOPE IN JUNCTION ASSUMED AS .01856 ENTRANCE LOSSES = 0.000 JUNCTION LENGTH(FEET) = 4.00 FRICTION LOSS = ,074 JLINCTION LOSSES = DY+HVl-H'J2+(FRICTION LOSS)t(ENTRANCE LOSSES) JUNCTION LOSSES = 1.381t 1.387- 1.473t( .074)t( 0.000) = 1.369 NODE 727.00 : HGL= < 377.685i;EGL= < 37Y.072;;FLOWLINE= < 374.230) """""""""""""""""""""""""~""""""""""""- PRESSURE FLOW PROCESS FROI.; NODE 729.00 TD NODE 728.00 IS COOE = 1 UPSTREAM NODE 728.00 ELEVATION = 375.34 ""~""""""_""""""""""""""""""""""~""""""- SIPE FLOLI = 16.X CFS PIPE DIAMETER = 18.00 INCHES CfiLCULATE PRESSURE FLOI? FRICT1OI.I LOSSES!LACFCD) : ;PE LENGTH = 27.25 FEET rwrdum N = .01200 HF=L+SF = ( SF=(Q.,%j**2 = I( 27.25)rt: ,0215362) = ,587 NODE 728.00 : HGL= < 378.272>;EGL= < 379.657);FLOWLINE= < 375.340i 16.70)/1: 113.797))*+2 = .02i53d2 --""""---""""--""""--"""-~"""""""""""~"""""-~ PRESSURE FLOIW PROCESS FROM NODE 728 .00 TO NODE 727.00 IS CODE = 5 UPSTREAM NODE 727.00 ELEVATION = 375.34 CALCULATE PRESSURE FLOW JUt4CTION LOSSES: NO. DISCHARGE DIAMETER AREA VELOCITY DELTA 1 HU 9.8 18.00 2 16.7 18.00 1.767 5.546 1 i ,500 1.767 9.450 .478 i ,387 3 4 0 .!I 0.0 0 .00 0 ,000 0 ,000 0 .00 0 .@00 0.000 - 0.000 0 .000 5 6.?===Q5 EQUALS BASIN INPUT=== " - LACFCD AND OCEMA PRESSURE FLOW JUNCTION FORMULAE USED: DY=102*'J2-Q1*'Jl*COS(~ELT~l~-Q3~!~3*COS(DELTA3~- Q4*V4rCOSIDELTA4))/~~AltA2~*16.1) UPSTREAM MANNINGS N = .01200 UPSTREAM FRICTION SLOPE = .00742 DOWNSTREAM MANNINGS N = .01200 -~lJNSTREAH FRICTION SLOPE = ,02154 .,JERAGED FRICTION SLOPE IN JUNCTION ASSUMED AS .01448 JUNCTION LENGTH(FEET? = 4.00 FRICTION LOSS = ENTRANCE LOSSES = .277 ,058 JUNCTION LOSSES = DYtH'Jl-HV2t(FRICTION LOSS)tIENTRANCE LOSSES) NODE 727.00 : HGL= < 380.445j;EGL= .: 380.723j;FL@bllLINE= < 375.340:: JUNCTION LOSSES = I .83st ,478- 1.3wt( .o5a:)t( ,277) = 1,264 ............................................................................ PRESSURE FLOW PROCESS FROM NODE 727.00 TO NODE 725.00 IS CODE = 1 UPSTREAM NODE 725.00 ELEUATI ON = 389,86 ...................................... CALCULATE PRESSURE FLOW FRICTION LOSSESILACFCD): PIPE FLOW = 9.80 CFS PIPE DIAMETER = 18.00 INCHES ,"PE LENGTH = 85.40 FEET MANNINGS N = .01200 HF=L*SF = < 85.40)rI ,0074163) = .633 NODE 725.00 : HGL= < 381.078);EGL= < 381.556);FLOWLINE= < 389.860) =IQ/K)**2 = (< 9.80!11 113.797))**2 = .0074163 PRESSURE FLOW ASSLIMPTION USED TO ADJUST HGL AND EGL LOST PRESSURE HEAD USING SOFFIT CONTROL = NOLIE 725.00 : HGL= < 391,36~0?;EGL= < 391.838);FLOWLINE= < 389.860) 10.28 ....................................... "~"""""""_""""""""""""""""""""""""""""" PRESSLIRE FLOW PROCESS FRO:..? NODE 725.00 TO NODE 724 .00 IS CODE = 5 UPSTREAM NODE 724.00 ELEVATION = 389.86, CALC.ULATE PRESSURE FLOlnl JUNCTION LOSSES: NO. DISCHARGE DIAMETER AREA VELOCITY DELTA 1 9.8 18.00 1 .767 5.546 42.000 ,478 3 2 9.8 18.00 1 .767 5.546 " .478 0.0 0 .no 4 0 .o 0 .000 o.uno 0 .000 0 .00 0 .000 0.000 0 .no0 5 0 .@===OS EQUALS BASIN INPUT=== HI,! - - LACFCO AND OCENA PRESSLIRE FLOW JUNCTION FORMULAE USED: DY=IQ2xV2-QlxVlfCOSIDELTAl~-Q3*~~~3fCOS1DELTA3)- Q4*U4*COS~DELTA4~~).~~1AltA2)*16.1) - UOWNSTREAM MANNINGS N = .01200 'STREAM MANNINGS N = .Dl200 UPSTREAM FRICTION SLOPE = .00742 AVERAGED FRICTION SLOPE IN JUNCTION ASSUMED AS ,00742 DOlnlNSTREAM FRICTION SLOPE = .00742 JLP.ICT1Ot.i LENGTHIFEET) = 4.00 FRICTION LOSS = ,030 ENTRANCE LOSSES = 0 ,000 NODE 724.00 : HGL= < 3?1.6.35!;EGL= < 392.113);FLOWLINE= < 389.86CIj JUNCTION LOSSES = .245t .478- .478+I .030)tI 0.000, = .275 JUNCTION LOSSES = DYtHVl-HV2t(FHICTJON LOSS)+IENTRANCE LOSSES:) ....................................... ...................................... PRESSURE FLU!! PROCESS FROM NODE 724.00 TO NODE 723.00 IS CODE = 1 UPSTREAM NODE 723.00 ELE?JATION = 391 .47 CALCULATE PRESSURE FLOW FRICTIOK LOSSES1LACFCD) : PIPE FLOW = PIPE LENGTH = 9.80 CFS PIPE DIAMETER = le.00 INCHES SF=lQ./K)**2 = I< 70.00 FEET ?.80)/< 113.797))*+2 = .a074163 HF=L+SF = < 70.00)*i .0074163) = NODE 723.00 : HGL= < 392.154>;EGL= < 392.632j;FLOWLINE= < 391.470) .519 PRESSURE FLOW ASSUMPTION LISED TO ADJUST HGL AND EGL LOST PRESSLIRE HEAD USING SOFFIT CONTROL = -82 """""""""_""""""""""""""""""""""""""""~ MANr$Irm rd = ,01200 ...................................... -7DE 723.00 : HGL= < 392.970);EGL= < 393.448);FLOWLINE= < 391.470) """""""""_""""""""""""""""""""""""""~"" ....................................... PRESSLIRE FLOW PROCESS FROM NODE 723.00 TO NUDE 722.00 IS CODE = 5 LIPSTREW NODE 722.00 ELEVATION = 391.47 ........................................ CALCLILATE PRESSURE FL ~ILI .IIN~TI~N I nwFs! hq~. O;SC~;?R~E DIdyCTER AREA vfim~f ~- +t-~~-~-----#(t ~~ ~ 1 9.8 lR.@O 2 9.8 1.767 5.54t. 45.800 16.0iI 1.767 5.546 .478 3 0.0 .4?8 0 .on 3 0 .@00 0.000 0.0 0 .000 0 .OO 0 .000 0.00O 0 ,000 - 0 .0===Q5 EQUALS BASIN INPUT=== " - r .g - .iFCD AND OCEMA PRESSURE FLOlJ JUNCTION FORMULAE USED: DY=~Q2*'~/2-Ql*Ul*COSIDELTAl)-Q3+'~~3iCOS~DELTA3!- R4iV4*COS~DELTA4:!),/(~Al+A2~*16.1! UPSTREAM MANNINGS N = .0120@ UPSTREAM FRICTION SLOPE = ,00742 AVERAGED FRICTION SLOPE IN JUNCTION ASSUPIED AS ,00742 DOWNSTREAM FRICTION SLOPE = ,00742 JUNC.TION LENGTH(FEET:I = 4.00 ENTRANCE LOSSES = 0.000 FRICTIOf.1 LOSS = .030 DOLJNSTREA;M MANNINGS N = ,01200 JUNCTION LOSSES = DYtHU1-HU2t~FRICTION LOSS!+IENTRANCE LOSSES! JUNCTION LOSSES = .289t ,478- .478tI ,030)tI 0.000) = ,319 NODE 722.00 : HGL= < 353.289i;EGL= < 393.766>;FLOWLINE= < 391.47O:) ...................................... ...................................... PRESSURE FLOld PROCESS FROM NODE 722.00 TO NODE 720.110 IS CODE = 1 UPSTREAM NODE 720 ,013 ELEVATION = 392.47 CALCULATE PRESSURE FLOiJ FRICTION LOSSESILACFCD! : PIPE LENGTH = 91 .OO FEET SF=(Q.,'K:)**2 = (I 9.80:)/( 113.797!)**2 = .00?4163 .M=L*SF = ( 91 .00)*I .0074163:) = .675 ....................................... PIPE FLOW = 9.80 CFS PIPE DIAMETER, = 1P.OD INCHES rlAw4INeS 1.1 = ,01200 DE 720.00 : HGL= < 393.964>;EGL= < 354.441);FLOWLIF.IE= < 392.470:; """""""""_""""""""""""""""""""""""""""~ """"""""_"""""""""""""""""""""""""""""~ PRESSURE FLOU PROCESS FROM NODE 720 .00 TO NODE 719.00 IS CODE = 5 UPSTREAM NODE 71fi.00 ELE'JATION = 352.47 CALCULATE PRESSURE FLDI JUNCTION LOSSES: NO. DISCHARGE DIAMETER AREA VELOCITY DELTA H'J 1 9.8 18.00 1 .767 5.546 42 I 200 .47P 2 ?.8 16.00 1.767 5.546 " .478 3 0.0 0 .OO 4 0 .OD0 0 .0 0 .nu 0 .on0 0 .000 - 0 .000 0 .000 0 .000 5 0 .@===a5 EQUALS BASIN INPUT=== - LACFCD AND OCEMA PRESSURE FLOW JUNCTION FORMLILAE USED: DY=(Q2~Y2-~l*Vl+COSIDELTAl~-Q3i~~3*COSIDELTA3!- Q4*U4iCOSIDELTA4! !/( !A1 tA21 il6.1 j UPSTREAV MANNINGS N = .01200 -STREAll FRICTION SLOPE = .O0742 A'JERAGED FRICTION SLOPE IN JU14CTJON ASSUMED AS ,013742 JUIKTICW LENGTH(FEET) = 4.00 ENTRANCE LOSSES = 0.000 FRICTION LOSS = . 030 DOWNSTREAM tvwdIrm r4 = ,0120o .&INSTREAM FRICTION SLOPE = .O0742 JlIt.ICTI0N LOSSES = DYtHVl-H!1Zt(FRIC.TIO1~ LC\55)t(ENTRANCE LOSSE:,.I JUt4CTIO1.1 LDSSES = .246+ ,478- .478t( .030:!tI n.000) = .277 NnnF 71q.nr1 ! Hr:l= < 194~747.;:~r3= / ?GA ~~C.\.FICII.III~JE= t 207 47rt', "_ " """""""""""""""""""""""~~~~~~"""""""""""-~ """""""-"""""""""""""""" PRESSLIRE FLOU PROCESS FROH NODE 719.00 TO NODE 710.00 IS CODE = 1 UPSTREAEI NODE 710.00 ELEVATION = 404.44 CALCULATE PRESSURE FLOIA FRICTION LOSSESCLACFCD:]: EIPE FLON = 9.80 CFS PIPE DIAMETER = 18.00 INCHES """"""""""""""""""""""""""~"""""""""""- 'E LENGTH = 57.00 FEET MANNINGS N = .01200 2<=IR./K)3*2 = (I 9.80)/( 113.797))**2 = .0074163 HF=L+SF = I 57.00)*( ,0074163) = NODE 710.00 : HGL= < 394.670?;EGL= < 395.148?;FLOldLINE= < 404.440) ,423 LOST PRESSURE HEAD USING SOFFIT CONTROL = PRESSURE FLOW ASSUMPTION USED TO ADJUST HGL AND EGL 11.27 NODE 710.00 : HGL= < 405.940?;EGL= < 406.418);FLOWLINE= < 404.440> ........................................ ........................................ PRESSURE FLOM PROCESS FROM NODE 710 -00 TO NODE 709 .@@ IS CODE = 5 UPSTREAEI NODE 709. 00 ELEVATION = 404.44 ........................................ CALCULATE PRESSURE FLOLJ JUNCTION LOSSES: NO. DISCHARGE DIAMETER AREA VELOCITY DELTA HV 1 5.1 18.00 1.767 2,886 45.000 ,129 2 ?.S 18.00 1 ,767 5.546 " ,478 3 4.7 18.00 1 ,767 2.660 90.000 4 0.0 0 -00 0 .000 0 ,000 0 .000 d 0 .G===Q5 ERUALS BASIN INPUT=== n - - c LACFCD AND OCEMA PRESSURE FLOW JUNCTIO1.I FORMULAE USED: DY=!02*'~!2-~1~'~~1*COSIDELTAl~~-R3*'J3*CO~~DELTA~~- 04+V4+COSIDELTA4!j/~~AltA2:)*16.1) - .'STREAM MANNINGS N = .01200 DOldNSTREAH MANNINGS t4 = .0 1200 UPSTREAM FRICTION SLOPE = .00201 AVERAGED FRICTION SLOPE IN JUNCTION ASSUMED AS .00471 DOl.Jt4STREAM FRICTION SLOPE = ,00742 JUNCTION LENGTHCFEET) = 4.00 ENTRANCE LOSSES = 0.000 FRICTION LOSS = .019 JUNCTION LOSSES = DYtH111-HV2+IFRICTIOF4 L@SS)t<ENTRANCE LOSSES) JUNCTION LOSSES = .772+ .129- .47St( .019)t( 0.000) = -443 NODE 709.00 : HGL= < 406.73!);EGL= < 406.860>;FLOWLINE= ( 404.440:) ........................................................................ PRESSURE FLOIW PROCESS FROM NODE 709.00 TO NODE 705.00 IS CODE = 1 UPSTREAM NODE 705.00 ELEVATION = 420.98 CALCULATE PRESCURE FLON FRICTION LOSSES(LACFCL0: PIPE FLOW = 5.10 CFS PIPE DIAMETER = 18.00 INCHES PIPE LENGTH = 106.73 FEET MANNINGS N = .01200 SF=IQ/K!**2 = I( 5.10!/( 113.797)j**2 = .0020085 NODE 705.00 : HGL= < 406.945>;EGL= < 407.075>;FLOWLINE= ( 420.980) HF=L*SF = ( 106.73!*( .0020085) = .214 """""""""""""""""""""""""""""""~""""""- ...................................... PRESSURE FLOW AssurIPTIOrd USED TO ADJUST HGL AND EGL LOST PRESSURE HEAD USING SOFFIT CONTROL = 15.53 )DE 705.00 : HGL= < 422.480?;EGL= < 422.6[19>;FLOlJLlNE= < 420.980) ................................................................ PRESSURE FLOld PROCESS FROM NODE 705.00 TO NODE 704.00 IS CODE = 8 UPSTREAM NODE 704.00 ELEVATION = 420.98 ""~"""""""""""""""""""""""""""""""""""- ~ ~~ ~ ~ ~~ ~- UPSTREAY NODE 704.00 PRESSURE FLOW PROCESS FROH NOPE 705.00 TO NUDE 704.00 IS CODE = 8 ELEVATION = 420.9s CALCULkTE PRESSURE FLOW CATCH BASIN ENTRANCE LOSSES(LACFCD:I : ....................................... --~~-~~~,~€~--------~;~-~---B-IP~-MA)~EKR"~~~~~~=--~~,OU " YSSURE FLOW VELOCITY HEAP = .12Y NODE 704.00 : HGL= < 422.635?;EGL= < 422,P3:);FL@I..~LI~.1E= < 420.980) ,.,+TUH BASIN ENERGY LOSS = .2*<VELOCITY HEAD) = .2*! ,129) = .02P EN@ OF PRESSURE FLOW HYDRAULICS PIPE SYSTEM ...................................... ...................................... "" &78/ . L/a% E-z ............................................................................ /a 5"Z6-& PRESSURE PIPE-FLOW HYDRAULICS COMPUTER PROGRAM PFICKAGE - (REfErEnCE: LACFD,LACRD,& OCEM HYDRAULICS CRITERION! *r. i***~X*****t*~ti~~*~************i**************************************** (((((~~~<(<(~(((~(({(((~~~~(<((~~~(~(~>>)~)))~)))~)))>)))))))))?>~)))~~>~))> IC) Copyright 1982 Advanced Engineering Software CAESI Especially prepared for: MANITOU ENGINEERING COMPANY ({~(({(~(!{((('~((~(~((I~<~(~~~~~~~~~~>~)>>?~?))>~>)>))>)~??>~)>~?~>>j?:)j>>> ************Y************************************************i*****~******** NOTE: STEADY FLOId HYDRAULIC HEAD-LOSS COMPUTATIONS EASED ON THE HOST CONSERVATIVE FORMULAE FROM THE CURRENT LACRD ,LACFCD, AND OCEMA DESI c;rd MANUALS. NODE NUMBER = 119.00 DOldNSTREAH PRESSURE PI PE FLOW CONTROL DATA : FLOWLINE ELEVATION = 270.87 PIPE DIAMETERIINCH) = 18.00 ASSUMED DOWNSTREAM CONTROL HGL = 277.578 PIPE FL0LdICFS:l = 10.00 ...................................... ...................................... """"""""""""""""""""""~"""""""""""""""- ...................................... PRESSURE FLOlJ PROCESS FROM NODE 119.00 TO NODE 210.00 IS CODE = 1 UPSTREAM NODE 21 0.00 ELEVATION = 275.96 CALCULATE PRESSURE FLOId FR1C:TIOF.I LOSSESILACFCD) : PIPE FLOW = 10.00 CFS PIPE DIAMETER = 18.Ci0 INCHES PIPE LENGTH = 132.97 FEET rwmINc;E: rd = .01200 SF=(Q/K)**2 = I( 10.0O)/I 113.797))**2 = .0077221 HF=L+SF = I 132.77)*( .0077221) = 1 .@27 ....................................... NODE 210.00 : HGL= < 278.605>;EGL= < 279.102>;FLOWLINE= < 275.960) ....................................... ...................................... PRESSURE FLOlJ PROCESS FROM NODE 210.00 TO NODE 209.00 IS CODE = 8 UPSTREAM NODE 209 .OO ELEVATION = 275.96 PIPE FLOWICFS) = ALCVLATE PRESSURE FLOW CATCH BASIN ENTRANCE LOSSESILACFCD:) : 10.00 PIPE DIAMETERIINCH) = 18.00 PRESSURE FLOId 'JELOCITY HEAD = ,497 CATCH BASIN ENERGY LOSS = .2*IVELOCITY HEAD! = .2*I .497:1 = .OW - - """""""""""""""""~""""""""""""""""""""- ---""""""""""""""-"""""""""""""""""""""" NODE 209.00 : HGL= ( 279.202:);EGL= < 279.202>;FLOWLI~~IE= < 275.9C.U) citri ric CE'ECCIIDC CI nu u~.:n=:~.!II IPC ~TDC C.\,,CTC+.A ............................................................................ PRESSURE PI PE-FLOW HYDRAULI CS COMPUTER PROGRAM PACKAGE (Reference: LACFD,LACRD,& OCEMA HYDRAULICS CRITERION! * X**********************************************************************f ({((({{({({((({((((({{({({(({{{{{{(((~!))))))!))!)!?!??)})))!!)})}))))}:>!}}} - (C) Copyright 1982 Advanced Engineebing Software [AESI Especially prepared for: MANITOU ENGINEERING COMPANY ({(({(({{(({{{{{{{{({{({{(({{{((((((({}})):}!!jj!!))!j})!)!!}:>}))))})}}j)!)}! ............................................................................ NOTE: STEADY FLOW HYDRALILIC HEAD-LOSS COMPUTATIONS BASED ON THE MOST CONSERVATIVE FORMULAE FROM THE CURRENT LACRD,LACFCD, AND OCEMA DESI Grq twuALS. NODE NUMBER = 1046.00 DOWNSTREAM PRESSURE PIPE FLOW CONTROL DATA: PIPE DIAMETER(1NCH) = 18.00 FLOWLINE ELEVATION = 316.51 PIPE FLOW(CFS) = 8 -90 ASSUMED DOWIGTREAM CONTROL HGL = 321 ,521 ............................................................................ PRESSLIRE FLOW PROCESS FROM NODE 1046.00 TO NODE 1045.00 IS CODE = 1 LIPSTREAM NODE 1045.00 ELEVATION = 317.55 ...................................... CALCULATE PRESSURE FLOW FRICTION LOSSES(LACFCD): PIPE FLOW = 8.90 CFS PIPE LENGTH = PIPE DIAMETER = 18.00 INCHES SF=!Q/Kj**2 = (< 8.90)/! 113.797))**2 = ,0061167 NODE 1045.00 : HGL= ( 321.786>;EGL= ( 322.180);FLOWLINE= < 317.550> HF=L*SF = I 43.28!*( .0061167j = .265 43.28 FEET MANNINGS N = .01200 ...................................... PRESSURE FLOW PROCESS FROM NODE 1045.00 TO NODE 1044.00 IS CODE = 8 UPSTREAM NODE 1044.00 ELEVATION = 317.55 ...................................... - rIPE FLOlA!CFS) = CATCH BciSIN ENERGI LOSS = .2*(uELOCITY HEADj = .2*1 ,394) = .079 hLCULATE PRESSURE FLOW CATCH BASIN ENTRANCE LOSSES(LACFCD) : 8.90 PRESSURE FLO1.d VELOCITY HEAD = ,394 NODE 1044.00 : HGL= < 322.258);EGL= < 322.258);FLOI.~LINE= < 317.550) PIPE DIAMETER(1NCH) = 18.00 """""""""__"""""""""""""""""""""""""""" ...................................... occ- " E,W-CW-F'RE?%K-FL3i,? HiDF:AIJL I CS PI PE 5:'ISTEt.l .I ~ , I ..,, / / ............................... PRESSURE FLOhl PROCESS FROM NODE 1048.00 TO NODE 845.00 IS CODE = 1 UPSTREAM NODE 845.00 ELEVATION = 319.44 CALCULATE PRESSLIRE FLO!J FRICTION LOSSESILACFCD): PIPE FLOW = 6.60 CFS PIPE DIAMETER = 18.00 INCHES PIPE LENGTH = 37.10 FEET MANNINGS N = ,01200 SF=(Q/Kj**2 = (( 6.6@)/I 113.7?7)>**2 = ,0033638 HF=L*SF = I NODE 845.00 : HGL= < 327.580>;EGL= < 327.796>;FLOWLINE= < 319.440:> 37.10)*( ,0033638) = * 125 ....................................... CALCULATE PRESSLIFE FLolJ CATCH BASIN ENTRANCE LOSSESILACFCD) : PIPE FLOW(CFS) = 6.60 PIPE DIAMETERIINCH! = 18.00 PRESSURE FLOU VELOCITY HEAD = ,217 NODE 844.00 : HGL= < 327.84@>;EGL= < 327.840j;FLOWLINE= < 315.440) CATCH BASIN ENERGY LOSS = .P*(VELOCITY HEAD) = ,2*( ,217) = .043 ........................................ """"""""""~"""""""""""""""""""""""""""- -. ._ " -. -. . .,., ~ ~" _." d78/ 69446 g+5 PRESSLIRE PIPE-FLOU HYDRAULICS COMPUTER PROGRAM PACKAGE (Reference: LACFD,LACRD,& OCEMA HYDRAULICS CRITERION) * ........................................................................ - Especially prepared far: MANITOU ENGINEERING COMPANY ((((({((((((((((((((((((((((((((((((<(:)))~>>)j?)))))}>)?j:)???)j:))?}>?}:))))~> ............................................................................ NOTE: STEADY FLOL! HYDRAULIC HEAD-LOSS COMPUTATIONS BASED ON THE MOST DESIGN MANUALS. CONSERVATIVE FORMULAE FROM THE CLIRRENT LACRD,LACFCD, AND OCEMA DOlrlNSTREAfl PRESSURE PIPE FLOW CONTROL DATA: NODE NUM8ER = 82R -00 PIPE DIAMETER(1NCH:j = 18.00 FLOWLINE ELEVATION = 352.67 PIPE FLOI*I(CFS) = ASSUMED DOIJNSTREAM CONTROL HCiL = 358.010 6.30 ---------""-"-""""-""""""""""""""""""""""""" --------"""----""""""""~"""""""""~""""""""""" ....................................... PRESSURE FLOld PROCESS FROM NODE 825.00 TO NODE 780 .@O IS CODE = 1 UPSTREAM NODE 780.00 ELEVATION = 353.61 PIPE FLOW = CALCULATE PRESSURE FLOW FRICTION LOSSES(L4CFCD): PIPE LENGTH = 6.30 CFS 55.41 FEET PIPE DIAMETER = 18.00 INCHES SF=(Q.,'K)**2 = (< 6.30)/( 113.797))**2 = ,0030649 HF=L*SF = I: 55.41)*( ,0030649j = NODE 780.00 : HGL= < 358.180);EGL= < 358.377);FLOWLINE= < 353.610) .170 "" "_ ...................................................... ..................................................... UPSTREAM NODE 779.00 ELEVATION = 353.61 "-------""----"""""""""""""""""""""""""""""~ MArmIrm N = ,01200 PRESSURE FLad PROCESS FROM NODE 780.00 TO NODE 779.00 1s CODE = CgL~~~~~~ PRESSURE FLOW CATCH BASIN ENTRANCE LOSSES'LACFCD): PIPE DIAMETER<INCH) = 18.00 ~KESSURE FLOlJ UELOClTY HEAD = ,157 r.IODE 77y,oo : ( 3;g.q17);EGL= < 358.417);FLOh'L1r4E= ( 353'610? CATCH BASIN E~~ERE~ LOSS = .2*(VELOCITY HEAD) = -2,' "?" *03? 'E FLOWICFS) 6.30 ====="""" - ............................................ EN[) OF PRESSURE FLOI,J HYDRAULICS PIPE ............................................................................ PRESSURE FLOW PROCESS FROM NODE 729.00 TO NODE 748.00 IS CODE = 6 UPSTREAM NODE 748. 00 ELEVATION = 374.23 PIPE FLOW = CALCLILATE PRESSURE FLOW ANGLE-POINT LDSSESILACRD): PIPE ANGLE POINT DELTA = 10.00 DEGREES 13.90 CFS PIPE DIAMETER = 18.00 INCHES PRESSURE FLOW VELOCITY = 7.87 FEET/SEC. VELOCITY HEAD = -961 NODE 748.00 : HGL= < 377.714>;EGL= ( 378.675>;FLOWLINE= < 374.230) HAPT=KA*(VELOCITY HEAD) = l .0300)*( -961) = .029 """""""""""""""""""~""""""""""~""~"""""- PRESSURE FLOlJ ANGLE-POINT COEFFICIENT KA = ,0300 ...................................... ...................................... ?ESSURE FLOW PROCESS FROY NODE 748.00 TO NODE 747.00 IS CODE = 1 JPSTREAM NODE 747.00 ELEUATI ON = 387.46 ...................................... CALCVLATE PRESSURE FLOW FRICTION LOSSES(LACFCD:): PIPE FLOW = PIPE LENGTH = 13.90 CFS PIPE DIAMETER = 18.00 INC.HES 264.59 FEET SF=<Q/K)**Z = (I UF=I .%SF = i 13.90!/( 113.797!)**2 = .@149199 rIANmm rd = .01200 3Ad e,G'>*i nf AGiOOi = a OAO ........................................................................... PRESSURE FLOW PROCESS FROY NODE 748.00 TO NODE 747.00 IS CODE = 1 UPSTREAM NOPE 747.00 ELEVATION = 387.46 Lf'4LCULATE PRESSURE FLOW FRICTION LOSSESILACFCD!: _"""""""""_"""""""""""""""""""""""""""" =E FLOW = 13.90 CFS PIPE DIAMETER = 18.00 INCHES PE LENGTH = 264.59 FEET rlAtmIrm N = ,01200 SF=IQ/K)**2 = (I 13.90)/I 113.797))**2 = .014?1?? HF=L*SF = I ?t.4.5?)*< ,0149199) = 3.948 t*.%m~t&M=f38Em" """"""""""""""""""""""""""""""""""""---- PRESSURE FLON ASSUMPTION USED TO ADJUST HGL AND EGL LOST PRESSURE HEAD USING SOFFIT CONTROL = NODE 747.00 : HGL= < 388.960);EGL= < 38?.921);FLOI*ILINE= < 387.460) 7.30 ........................................................................... PRESSURE FLOIJ PROCESS FROPl NODE 747 .00 TO NODE 746.00 IS CODE 5 UPSTREAM NOPE 746.00 ELEVATION = 387.46 CALCULATE PRESSURE FLOlJ JUNCTION LOSSES: ....................................... NO. DISCHARGE DIAMETER AREA VELOCITY DELTA HO 1 2 8.5 18.00 1.767 4.810 20 .000 13.9 * 359 3 0 .0 0 .00 0 .ooo 0 ,000 4 0 .000 0 -0 0 .OO 0.000 0 .000 0.000 5 18.00 1 .767 7.866 " .?61 - - 5,4===m EOUALS msm INPUT=== LACFCD AND OCEMA PRESSURE FLOW JUNCTION FORMULAE USED: - DY=~Q2*Y2-Ol*Yl*COSIDELTAi~-Q3*V3~COSIOELTA3~- Q4*V4*COSIDELTA4))/((AitAZ)~i6.1) UPSTREAM MANNINGS N = ,01200 DOWNSTREAM MANNINGS N = .Dl200 UPSTREAM FRICTION SLOPE = ,00558 DOWNSTREAM FRICTION SLOPE = .014?2 AUERAGED FRICTION SLOPE IN JUNCTION ASSUMED AS ,01025 JUNCTION LENGTHIFEET) = 4.00 FRICTION LOSS = .041 ENTRANCE LOSSES = .1?2 JUNCTION LOSSES = UYtHUl-HV2tfFRICTION L0SS)tIENTRANCE LOSSES) JUNCTION LOSSES = 1.246t ,359- .961t< .041)tI .1?2) = ,878 NODE 746.00 : HGL= < 3?0,43?>;EGL= < 390.7??>;FLOWLINE= < 387.460) PRESSLIRE FLOlJ PROCESS FROM NODE 746 -00 TO NODE 745.00 IS COPE = 6 UPSTREAM NODE 745.00 ELEVATION = 387.46 ...................................... CALCULATE PRESSIJRE FLOlrl ANGLE-POINT LOSSESILACRD): PIPE FLOlJ = 8.50 CFS PIPE DIAMETER = 18.00 INCHES PRESSURE FLOlJ ANGLE-POINT COEFFICIENT KA = ,0300 PRESSURE FLOW VELOCITY = 4.81 FEET/SEC. VELOCITY HEAD = .35? HAPT=KA*<UELOCITY HEAD) = I .0300)*I .359) = ,011 PIPE ANGLE POINT DELTA = 10.00 DEGREES MODE 745.00 : HGL= < 390.450);EGLz < 3?0.809);FLOULINE= < 387,460) ................................. ...................................... PRESSLIRE FLOW PROCESS FROM NODE 745.00 TO NODE 744 -00 IS CODE = 1 UPSTREAM NOPE 744, 00 ELEVATIOr~I = 392.1P CALCULATE PRESSLIRE FLOW FRIC.TIClN LOSSESILACFCD) : ....................................... ................................... PRESSURE FLOW PROCESS FR@"I NODE 745.00 TO NODE 744.00 IS CODE = 1 UPSTREAM NODE 744 -00 ELEVATION = 392.39 PIPE FLOW = CALCULATE PRESSURE FLOld FRICTION LOSSES!LACFCD!: 8.50 CFS piGE LENGTH = 197.23 FEET PIPE DIAMETER = 18.00 INCHES MANNINGS N = .012@0 ...................................... lQ./K)**2 = (( 8.50)./( 113.797))**2 = .0055792 hr=L*SF = ( 197.23)*( .@OS57921 = 1 .lo0 NODE 744.00 : HGL= < 3?1.551>;EGL= < 391.910);FLOWLINE= < 392.190) PRESSURE FLOW ASSUMPTION USED TO ADJUST HGL AND EGL LOST PRESSURE HEAD USIN6 SOFFIT CONTROL = 2.14 NODE 744.00 : HGL= < 393.690>;EGL= < 394.049);FLOWLINE= < 392.190) ....................................... LACFCD AND DCEMA PRESSURE FLOW JUNCTION FORMULAE USED: DY=(Q2*'J2-~l*V1*COSiDELTA11-Q3*U3*COS!DELT~3~- Q4*'J4*COS(DELTA4!i/I!kl+A2)*16.1) - TREAM wtwrm rd = ,01200 . ANSTREAM MANNINGS N = .01200 UPSTREAM FRICTION SLOPE = ,00558 DOI.*INSTREAM FRICTION SLOPE = ,00558 AUERAGED FRICTION SLOPE IN JUNCTION ASSUMED AS .00558 JUNCTION LENGTH(FEE1) = 4.00 ENTRANCE LOSSES = 0.000 FRICTION LOSS = ,022 JLINCTION LOSSES = UYtH'J1-HV2t~FRICTIOr.I LOSS)+IENTRANCE LOSSES) JUNCTION LOSSES = .719t .359- .359+( .022!+( 0.000) = ,741 NODE 743.00 : HGL= < 394.431>;EGL= < 394.790>;FLOWLINE= < 392.130) CALCULATE PRESSURE FLOW FRICTION LOSSES!LACFCD) : PIPE FLOW = PIPE LENGTH = 8.50 CFS 27.25 FEET PIPE DIAMETER = 18.00 INCHES MANNINGS N = ,012013 SF=!Q./K:)**2 = I( 8.5@:1/< 113.797))**2 = .0055792 HF=L*SF = ( NODE 742.00 : HGL= < 394.583>;EGL= < 3?4.942>;FLOWLINE= < 392,600) 27.25)*( .0055792:) = .152 ...................................... PSSllRE FLOW PROCESS FROM NODE 742.00 TO NODE 741.00 IS CODE = 8 TREAM NODE 741 .00 ELEUATl ON = 3C2.6C1 ....................................... CALCULATE PRESSURE FLOW CATCH BASIN ENTRANCE LOSSES(LACFCD) : PIPE FLOlnl(CFC,) = 8.50 PRESSURE FLOlhl UELOCITt HEAD = .359 PIPE DIAMETER!INCH) = 16.00 CATCH fiASIN ENERGY LOSS = .2*!UELOCITY HEAD) = ,?*I ,359) = .07i *,nnr 7". . ,,?.)~ , ~.~- *.A> "6 --- -,-. -. . --- ~ ~ NODE 743.00 : HGL= < 394.431>;tbL= < 3Y4./YU>;FLUWLINt= < ;JY2,IYU> ....................................... """""""""_""""""""""""""""""""""""""""~ PRESSLIRE FLOIW PROCESS FROM NDDE 743.00 TO NODE 742.00 IS CODE = 1 UPSTREAM NODE 742,0@ ELEVATION = 392.60 -_ LCLILATE PRESSURE FLOW FRICTION LOSSES( LACFCD) : PE FLOW = PIPE LENGTH = 8.50 CFS PIPE DIAMETER = 18.00 INCHES 27.25 FEET MAPJNINGS N = .@I200 HF=L*SF = ( SF=!WK)**2 = (! 27.25)*( .0055792) = 8.50:)/1 113.797))**2 = .0055792 NODE 742.00 : HGL= < 394.583>;EGL= < 394.942>;FLOlJLINE= < 392.600) .152 ...................................... PRESSURE FLOW PROCESS FROM NODE 742.00 TO NODE 741 .00 IS CODE = 8 UPSTREAM NOOE 741 .00 ELEVATION = 392.60 CALCULATE PRESSURE FLOW CATCH BASIN ENTRANCE LOSSES(LACFCD1: PIPE FLOW(CFS) = 8.50 PRESSURE FLOW VELOCITY HEAD = .359 PIPE DIAMETER(1NCH) = 18.00 CATCH RASIEJ ENERGY LOSS = .2*1UELOCITY HEAD) = .2w( ,359) = .072 NODE 741.00 : HGL= < 395.014);EGL= < 395.014i;FLMJLINE= < 392.600) """""""""_""""""""""""""""""""""""""""~ ....................................... END OF PRESSURE FLOl,.! HYDRALILICS PIPE SYSTEM ,- """""_""""""""""""""""""""""""""""""""- ...................................... PRESSURE FLOLJ PROCESS FROM NODE 759 -00 TO NODE 750 .0@ IS CODE = 1 UPSTREAM NODE 750 .00 ELE'JATION = 372.80 ""-""""-""""""""""""""""""""""""""""""" CALCULATE PRESSURE FLOW FRICTICtrJ LOSSES<LACFCD:> : PIPE FLOW = 25.10 CFS PIPE LENGTH = PIPE DIAMETER = 24.00 INCHES SF=IQ/K)**2 = (( 36.77 FEET rwrdIrm 14 = .OI~OCI HF=LrSF = ( NODE 750.00 : HGL= < 375.295:);EGLc < 376.286);FLOWLINE= < 372.80@? 25.10)/< 245.076!)**2 = .01048?3 3t.77!*( .0104393) = .386 ...................................... ...................................... PRESSURE FLOW PROCESS FROM NODE 750 .00 TO NODE 749.00 IS CODE = 5 UPSTREAM NODE 749.00 ELEVATION = 372.80 - - NO. DISCHARGE DIAMETER AREA VELOCIT'Y DELTA HI,, ILCULATE PRESSURE FLOW JLlE4CTI ON LOSSES: 1 2 25.1 24.00 45.000 .??l 25.1 3.142 7.9RO 24.00 3-14? 7 .990 " ,991 3 4 0 8 0 0 .(I0 0 . 0 0 .or1 0 .00CI 0.000 0 .000 0 . 0 0 0 0 .000 0 .00O - - " " ~ ~~ ~ - LACFCD AE4D OCEM4 PRESSURE FLOW JUNCTION FORMULAE USED: @Y'~~2*U2-Q1*Ul*COS(DELTAl~-Q3*U3*COS~DELTA3~- Q~*U~*C.OS(DELTA~:I~/~~A~+A~)*~~,~) UPSTREAM MANNINGS r4 = .01200 STREAM FRICTION SLOPE = .01049 .lJNSTREAM FRICTION SLOPE = .01049 - DOWNSTREAM MANNINGS N = .01200 AVERAGED FRICTION SLOPE IN JLNCTION ASSUMED AS .01049 JUNCTION LENGTH(FEET:j = 4.00 ENTRANCE LOSSES = 0.000 FRICTION LOSS = .042 JUNCTION LOSSES = @Y+HVl-HV2+(FRICTION LOSS)+(E14TRANCE LOSSES) JLlNCTIOt4 LOSSES = .581+ .991- .99lt( .042jt( 0.000) = ,623 NODE 749.00 : HGL= ( 375.917);EGL= ( 376,90R);FLOl,JL]NE= ( 372.800) PRESSLIRE FLOld PROCESS FROM NODE 749.00 TO NODE 778.00 IS CODE = 3 UPSTREAM NODE 778.00 ELEVATION = 373.27 ...................................... CALCULATE PRESSURE FLOW PIPE-BEND LOSSES(0CEMU:I: PIPE FLOW = 25.10 CFS PIPE DIAMETER = 24.00 INCHES PIPE LENGTH = 47.18 FEET MANNINGS N = .01200 CENTRAL ANGLE = 6,600 DEGREES VELOCITY HEAD = .991 FLOlJ UELOCITY = 7.99 FEET PER SECOND BEND COEFFICIENT(K8) = .Ot,77 HB=KB*(UELOCITY HEAD) = ( .068i*I ,991) = ,067 PIPE CONVEYANCE FACTOR = 245.076 FRICTION LOSSES = LaSF = ( FRICTION SLOPECSF) = .0104893 47.18)*1 .0104893) = .495 NODE 778.00 : HGL= < 376.479:!;EGL= ( 377.470);FLOWLINE= i 373.270) PRESSURE FLOl(1 AREA = 3.142 SQUARE FEET - " ...................................... PRESSURE FLOW PROCESS FROM NODE 778.00 TO NODE 777.00 IS CODE = 5 ' UPSTREAM NODE 777.00 ELEVATION = 373.27 ...................................... CALCULATE PRESSURE FLOW m4c:TI Or4 LOSSES: NO. DISCHARGE DIAMETER AREA VELOCITY DELTA HL' 1 8.5 18.00 1.767 4.810 2 25.1 24 -00 0 .0u0 3.142 .359 3 12.6 18.00 1 ,767 7. 990 ,991 7.130 4 4 ..0 71.200 - 5 18.00 1.767 2.264 45.000 - 0.0===R5 EQUALS BASIN INPUT=== " LACFCD AND OCEMA PRESSURE FLOInl JUNCTION FORMULAE USED: DY=(Q2*V2-Ql*Vl*COS(OELTAlj-Q3*U3*COS(DELTA3)- Q4*1~4*COS~DELTA4j!/~~AltA2~*16.1) uPsTREAr1 wwrdIr4G:i rd = ,01200 DOWNSTREAM MANNINGS N = ,01200 UPSTREAM FRICTION SLOPE = .00558 DOWNSTREAM FRICTION SLOPE = ,01049 A'JERAGED FRICTION SLOPE IN JUNCTION ASSLMED AS .00803 JUNCTION LENGTH(FEET) = 4.00 ENTRANCE LOSSES = 0 .000 FRICTION LOSS = ,032 JUNCTION LOSSES = DY+HUl-HV2t~FRICTION LOSS)+(ENTRAt.ICE LOSSES! JDE 777.00 : HGL= < 378.084i;EGL= ( 378.443:);FLOlJLI~4E= < 373.270) NCTION LOSSES = 1.573+ ,359- .Y91+( .03211+( 0.000j = .973 ...................................... ...................................... PRESSLIRE FLOW PRCICESS FROPI NO@E 777.00 TO NCIDE 772.00 IC, CODE = 3 UPSTREA!I N@[bE 772.00 ELE'JAT 1014 = 3811 .69 PIPE LENGTH = PIPE FLO!\l = 296.79 FEET 8.50 CFS PIPE DIAMETER = 18.00 INCHES MANNINGS N = .I31200 CENTRliL ANGLE = 53.100 DEGREES PRESSURE FLOI,.! AREA = 1.767 SQUARE FEET VELOCITY HEAD = ,359 FLOlJ UELOCITY = 4.81 FEET PER SECOND BEND COEFFICIENT(KB) = .1?20 -'=KB+(VELOCITY HEAD) = ( .192!+( ,359) = .I)&.? PE CONVEYANCE FACTOR = rRICTION LOSSES = L+SF = { 113.797 FRICTION SLOPE(SF! = 296.79)+< .0055792! = 1.656 NODE 772.00 : HGL= < 37?.809>;EGL= < 380.168:);FLOWLI~.IE= < ................................ PRESSURE FLOW ASSUMPTION USED TO ADJUST HGL Arm EGL LOST PRESSURE HEAD USING SOFFIT CMdTROL = 2.38 NODE 772.00 : HGL= < 382.190>;EGL= < 382.549:);FLOWLINE= < .0055792 380.690 > ...................................... ....................................... PRESSURE FLOiJ PROCESS FROll NODE 772.00 TO NODE 771 -00 IS CODE = 5 UPSTREAM NODE 771 .0@ ELEVATI ON = 380. 69 CALCLILATE PRESSURE FLmJ JLINCTION LOSSES: NO. DISCHARGE DIAMETER AREA VELOCITY DELTA H'J 1 8.5 18.00 1 s767 4.810 45.000 .-C 2 8.5 18.00 .&9 1.767 4.810 3 0 .0 0 .00 0 .on0 * 357 0.000 4 0 ,000 0 .0 0.00 0 .ct00 0 .000 0 .000 a .@===Qs EQUALS RASIrd IrwT=== " - c J - LACFCD AND OCEMA PRESSURE FLO1.d JUNCTION FORMULAE USED: DY=(02*V2-01*Vi+COSIDELTAl~-Q3*~~~*C@S{DELTA3!- Q4+V4*COSIDELTA4j~,/(~Al*A2~+16.1:) ,- STREAM MANNINGS N = ,01200 UPSTREAM FRICTION SLOPE = .00558 JWNSTREAM MANNINGS N = .01200 DOWNSTREAM FRICTION SLOPE = ,00558 AVERAGED FRICTION SLOPE IN JUNCTION ASSLIMED AS .00558 JUNCTION LENGTH(FEET! = 4.00 FRICTION LOSS = ,022 ENTRANCE LOSSES = 0.0U0 JUNCTION LOSSES = DYtHVl-HVZ+!FRICTION LOSS!+!ENTRANCE LOSSES) JUNCTIOtd LOSSES = .210+ ,359- .35YtI .022)*I 0.000) = .233 NODE 771.00 : HGL= < 382.423);EGL= < 382.782);FLOWLINE= ( 380.690i ...................................... ...................................... UPSTREAM NOOE 770.00 PRESSURE FLOlJ PROCESS FROM NODE 771 .00 TO NUDE 770.00 IS CODE = 1 CALCULATE PRESSURE FLOIU FRICTION LOSSES(LACFCD): PIPE FLOlJ = 8.50 CFS PIPE DIAMETER = 18.00 INCHES PIPE LENGTH = 38.54 FEET SF=IQ/K:)++2 = (( HF=L*SF = < 38.54)*! ,0055792) = .215 ELEVATION = 380 .?2 ....................................... r1ArwIms rd = .01200 8.50)/i 113.797))+*2 = ,0055792 NODE 770.00 : HGL= < 382.638>;EGL= < 382,9?7j;FL@WLINE= ( 380.920) '"ESSURE FLOW PROCESS FROM NODE 770.00 TO NODE 769.00 IS CODE = 8 STREAM NODE 769.130 ELElJATIO14 = 380 .92 --------------""~""""""""""~"""""""""""""""""" CALCULGTE PRESSURE FLOU CATCH BASIN ENTRAI.ICE LOSSES(LACFCDj : PIPE FLOW(CFS) = 8.50 PIPE DIAMETER<Ir.ICH! = 18.00 PRESSURE FLOW VELOCITY HEAD = ,359 NnnF 7.49 nn . UCI- , -01 o~~\_~~.~- I --- nlnjrl nltI I --- ---... CATCH BASIN ENERGY LOSS = .ZnIVELOC.ITY HEAD) = .2+( .35'?) = .@72 45/ L/W E-6 ............................................................................ AS& f26-& PRESSURE PIPE-FLOld HYDRAULICS COMPUTER PROGRAM PACKAGE - (Reference: LACFD,LACRD,h OCEEIA HYDRAILILICS CRITERION) ............................................................................ <((I{(((({(I{{({{{(({II{{{I{{(I{{{{I{{):)))))))>)))):)))j)))))j~?:))>j)))??)jj) (C:I Copyright 1982 Advanced Engineering Software IAESI Especially prepared for: MANITOU ENGINEERING COMPANY ((I(((((<{(<{((((<(I{{{({{{({{{I{II{{I);)j)j)j~):))))))))))))~))))):)~)j)j)>j)j ............................................................................ NOTE: STEADY FLOld HYDRAULIC HEAD-LOSS COMF'UTATIONS BASED ON THE ElClST CONSERVATIVE FORMULAE FROM THE CURRENT LACRD, LACFCD, AND OCEFIA DESI EN rIArwu, NODE NUMBER = 777.00 DOWNSTREAII' PRESSURE PIPE FLOlnl CONTRUL DATA: FLOWLINE ELEVATION = 373.27 PIPE DIAMETERIINCH) = i'Z.@@ PIPE FLOI.diCFS:l = 12.60 ASSUMED DOILJNSTREAPl CONTROL HGL = 378.084 ...................................... ...................................... ....................................... ...................................... PRESSURE FLOW PROCESS FRMl NODE 777.00 TO NUDE 774.00 IS CODE = 1 UPSTREAM NODE 774.00 ELEVATION = 373.53 ....................................... CALCULATE PRESSIURE FLUW FRICTION LOSSESCLACFCD!: PIPE FLOlJ = PIPE LENGTH = 12.60 CFS 28.78 FEET PIPE DIAMETER = 18.00 INCHES SF=(Q./Kjr*2 = (( HF=L*SF = I 12.60:1/! 113.797))**2 = ,0122596 28.78)*! .01225?6) = NODE 774.00 : HGL= < 378.437);EGL= < 379.226);FLOWLINE= < 373.530) .353 EIANNINGS rd = .OIZUO ...................................... ...................................... PRESSURE FLO1.d PROCESS FROM NODE 774.00 TO NODE 773.00 IS CODE = 8 YPSTREAM NODE 773.00 ELEVATION = 373.53 ~ bALCULATE PRESSURE FLUIJ CATCH BASIN ENTRANCE LOSSESCLACFCD) : PIPE FLOWrCFS) = PRESSIURE FLCtld VELOCITY HEAD = ,789 12.60 PIPE DIAMETER(1NCH) = 18.00 CATCH BASIN ENERGIi LOSS = .2*IUELOCITY HEAD) = .2*( ,789) = ,158 NODE 773.00 : HEL= < 375.384:>;EGL= < 379.384>;FLOWLINE= < 373.530, "-"""""-""""""""""~""""""""""""""""""""~ -----""""""""""""""""""""""""""~""""""""" .-.... -.r "~-~ -. .. ~ ***********X************************S*************************************** NOTE: STEAD;/ FLOIU HYDRAULIC HEAD-LOSS COMPUTATIONS BASED ON THE MOST CONSERVATIVE FbRMLILAE FROM THE CURRENT LACRD,LACFCD, AND OCEMA DESIGN MANUALS. NODE NUMBER = 777.00 DOWNSTREAEI PRESSURE PIPE FLOW CONTROL DATA: PIPE DIAMETER(1NCH) = 18.00 PIPE FLOW(CFS:) = 4.00 ASSUMED DOWNSTREAEl CONTROL HGL = 378.084 FLOWLINE ELE'JATI ON = 373.27 ...................................... ...................................... ...................................... PRESSURE FLOW PROCESS FROM NODE 777.00 TO NODE 776.00 IS CODE = 1 llPSTREAM NODE 776.00 ELEVATION = 373.79 CALCULATE PRESSURE FLOW FRICTION LOSSES(LACFCDj: PIPE FLOW = PIPE LENGTH = 4.00 CFS 13 I 08 FEET PIPE DIAMETER = 18-00 INCHES MANrwGS rq = .01m SF=(D/K:>**2 = (( 4.00>/( 113.797>)**2 = ,0012355 HF=L*SF = ( 13.08!*< .0012355) = .Old NODE 776.00 : HGL= < 378.100i;EGL= < 378,18O);FLOWLINE= < 373,790) ...................................... """""""""_""""""""""""""""""""""""""""~ ...................................... PRESSURE FLOW PROCESS FROM NODE 776.00 TO NODE 775.00 IS CODE = 8 JPSTREAM NODE 775.00 ELEVATION = 373.79 - .................................... LALCULATE PRESSLIRE FLOl.4 CATCH BASIN ENTRANCE LOSSESILACFCD) : PIPE FLOIJ!CFS:) = 4.00 PRESSURE FLOW VEL0C:IT.Y HEAD = .080 PIPE DIAMETER(INCH! = 18.00 CATCH B4SII.l ENERGI LOSS = .Z+!VELOCITi HEAD:) = .2*( ,080) = .016 NODE 775.@0 : HGL= ( 378.1Y!,i;EGL= ( 378.196);FLOWLINE' < 373.790) c.,n nr "" -,." _. _. . ... ... ." __" ",-".a /sf 5& 9-26 -& ............................................................................ ' PRESSURE PIPE-FLOW HYDRAULICS CMlPUTER PROGRAM PACKAGE - . (Reference: LACFD,LACRD,& OCEMA HYDRAULICS CRITERION! ............................................................................ (((({(((((((!((((((({{((({((({((((((({))>))))))?)))))))>)))))))))))}}))))))> iC! Copyright 1982 Advanced Engineering Software [AESI Espec ial 1 y prepared f,or : MANITOU ENGINEERING COMPANY ({((((!i!i{(((<(((((({{{({{{({{{{((({(~:)?)))?)))}>))))?)?)))))))))j)?))>)))? ............................................................................ NOTE: STEADY FLOIJ HYDRAULIC HEAD-LOSS COMPUTATIONS BASED ON THE MOST CONSERVATIVE FORMULAE FROM THE CURRENT LACRD ,LACFCD, Arm OCEMA DESIGN wwuALs, DOlJNSTREAM PRESSURE PIPE FLOlJ CONTROL DATA: NODE NUMRER = 709.00 FLOWLINE ELEVATION = 404.44 FIFE DIAMETER(1NCHj = 18.00 PIPE FLOIJiCFS:) = ASSUMED DOlJNSTREAM CONTROL HGL = 406.731 4.70 ....................................... ...................................... ............................................................................ PRESSURE FLOW PROCESS FROM NODE 709.00 TO NODE 715.00 IS CODE = 1 UPSTREAM NODE 715.00 ELEVATION = 404.98 CbLCULATTE PRESSURE FLOId FRICTION LOSSES(LAC.FCD) : PIPE FLOId = 4.70 CFS PIPE DIAMETER = 18.00 INCHES PIPE LENGTH = 23.62 FEET MANrdIwS rd = .OIZOO SF=(Q/K)**2 = (I 4.70:)/( 113.797))**2 = .0017058 NODE 715.00 : HGL= < 406.771);EGL= < 406.881>;FLOlALINE= < 404.980! HF=L*SF = ( 23.62)*( .0017058) = .040 ...................................... ...................................... ....................................... PRESSURE FLOW PROCESS FROM NODE 715.00 TO NODE 714.00 IS CODE = 8 - UPSTREAM NODE 71 4.00 ELE'JATION = 404.98 - ALCULATE PRESSURE FLOl4 CATCH BASIN ENTRANCE LOSSESILACFCD! : PIPE FLOW(CFS! = PRESSLIRE FLOIJ VELOCITY HEAD = .110 4.70 PIPE DIAMETER(1NCH) = 18.00 CATCH BASIN ENERGY LOSS = NODE 714.00 : HGL= < 406.903);EGL= ( 406.903);FLOWLINE= < 404.980:) .2*(VELDCITY HEAD! = .2*( .110! = ,022 ........................................... rTh.,T\ nc c,DrCCI,r,r r, I,. .,.. ..I I.. ." "" CC:! Copyright 1982 Advanced Engineering Software [AESI Especially pvepared for: MANITULI ENGIE4EERlNG COMPAtJY (((<({,~iii(i;i!.~i!!<(;(i(cl((((({{({({))~:)}):)}i))}?~):?}))))i~)?):~~?)}}))i)~) *******XX**X*******************************************~***~**************** NOTE: STEADY FLOU H'~DRALILIC HEAD-LOSS COMPUTATIONS BASED ON THE MOST CONSERVATIUE FORMULAE FROM THE CURRENT LACRD ,LACFED, AND OCEMA DESIGN MANUALS. NODE NUMBCR = 148 .00 DOW4STREAM PRESSLIRE PIPE FLCt.J CCNTRDL DATA: PIPE CIIAMETER!It.ICH:! = 30 .00 PIPE FLOIJIiC:FS) = ASSUHED DOIANSTRE4rS CONTROL HGL = 217.61@ 52.70 FLOlk!LINE ELE'~.JATlON = 215.11 ...................................... .................................... "- PRESSLIRE FLOW PROCESS FROM NODE 148.00 TO NODE 147 .0@ IS CODE = 1 UPSTREAP? NODE 147.00 ELEVATION = 226.66 PIPE FLOld = CALCULATE PRESSURE FLO1.d FF.ICT10P.1 LOSSES(LACFCD): 52.70 CFS PIPE LENGTH = 77.00 FEE? PIPE DIAMETER = 30.00 INCHES SF=!Q/K)**2 = (( 52.70:1./! 444.352:):!**2 = .014065Y NODE 147.00 : HGL= < 218.6?3);EGL= ( 220.483);FLOWLINE= < 226.660) HF=L*SF = 77.00:1*1 .014065Y:1 = 1 .083 PRESSURE FLOW ASSUMPTI0!4 USED TO ADJUST HGL AND EGL LOST PRESSURE HEAD USING SOFFIT CONTRCIL = 10.42, NODE 147.00 : HGL= < 22?.160?;EGL= ( 230.950>;FLOWLINE= i 226.660: ...................................... MAN:\III.!GS rq = .n1200 ...................................... _- ...................................... ...................................... PRESSURE FLO1.I PROCESS FROM NODE 147.00 TO NODE 147-10 IS CODE = 5 UPSTREAM NODE 147.10 ELE?IATION = 226.66 CALCULATE PRESSLIRE FLCU JIINCTI ON LOSSES: ....................................... NO. DISCHARGE DIAPIETER AREA VELOCITY DELTA H!.' ~~ ~ ............................................................................ PRESSURE FLOlil PROCESS FRO14 NODE 147.10 TO NODE 144 .O@ IS CODE = 1 UPSTREMI NODE 144.00 ELEOATI@N = 245.58 ,LALCULATE PRESSURE FLO:,d FRICTION L@SSES!LACFCD:) : -"""""""""_""""""""""""""""""""""~"""""- PE FLOU = 52.70 CFS PIPE @LAMETER = 30.00 INCHES r 1 PE LENGTH = 44 .00 FEET MAEWINGS rd = .O~ZOO SF=(O,/Kj+x2 = (( HF=LISF = ( NODE 144.00 : HGL= $ 230.315);EGL= < 232.104i;FLOWLINE= < 245.580? PRESSURE FLOIM ASSUMPTION USED TO ADJUST HGL AND EGL NODE 144.00 : HGL= < 248,08D>;EGL= < 249.87@);FLOlJLINE= < 245.520) 52.70:Wi 444.352))*+2 = .0140659 $4.0@)+< .014i1659) = ,619 ....................................... LOST PRESSURE HEAD uslrdc. SOFFIT CONTROL = 17.77 Y NO. CjiSCHARGE DIAMETER 1 51.2 30.00 2 3 52.7 30.00 0.0 4 0.0 0 .OO 0 .00 5 1 .5===Q5 EQUALS AREA UELOCITV DELTA H'J 4.909 10.430 0 .000 1 .683 4.909 10.73h 0 .000 " 1.790 0 .000 0 .oon 0.0@0 0 .000 0 .000 - - BASIN INPUT=== UPSTREAM MANNING5 N = .I31200 LIPSTREAP1 FRICTION SLOPE = .0132P DOWNSTREAH FRICTION SLOPE = .01407 AVERAGED FRICTION SLOPE IN JUNCTION ASSUMED AS .01367 JUNCTION LENGTHIFEET! = 4.00 FRICTION LOSS = ,055 DOl>lNSTRE4Jl, MANNINGS N = ,01200 r !TRANCE LOSSES = ,dNCTION LOSSES = D(tHUl-HV2trFRICTIOIJ LOSS!t(ENTRANCE LOSSES! JUNCTIO:.I LOSSES = ,201t 1.689- 1 .i70+i .055)+( ,358) = .513 NODE 144.10 : HGL= < 248,&94:>;EGL= < 25@.?83?;FL@lJLINE= < 245.580) .35e. CALCVLATE PRESSURE FLOW FRICTION LOSSESILACFCD!: PIPE FLEJ = 51.20 CFS PIPE LENGTH = 68.50 FEET MANI4INGS N = .01200 PIPE DIAMETER = 30.00 INCHES SF=<Q./K)x+2 = (< HF=L*SF = I 51.20>./< 444.352>)++2 = ,0132766 68.50)*{ .0132766! = NODE 142.50 : HGL= < 249.603>;EGL= ( 251.292?;FLOWLINE= < 267.500) .p09 """""""""^""""""""""""""""""""""""""""~ PRESSLIRE FLOW ASsmmIOr~ USED TO ADJUST HGL AND EGL LOST PRESSURE HEAD USING SOFFIT CONTRPL = 20 -40 NODE 142.00 : HGL= < 27@.000i;EGL= < 271.689);FLOWLINE= < 267.50CO ....................................... """"""""_""""""""""""""""""""""~""""""" PRESSURE FLOW PROCESS FROH MODE 142.00 TU NODE 142.10 IS CODE = 5 UPSTREAM NODE 142.10 ELEVATION = 267.50 ...................................... NO. DISCHARGE DIAMETER AF:EA VELOCITY DELTA Hu .LCULA?E PRESSURE FLCUd JUNCTION LOSSES: 1 51.2 30 .OO 4.90P 1c:.4317 24 ,000 1 .68? 2 -61 ,2 30 .OD 4.907 10.430 " 1 .&E7 3 0.0 0 .00 0 .000 0 .@!IO 0 ,000 4 0 '0 0 .00 0.000 0 ,000 0 ,000 - 4 0 .@===a5 EOIJALS RnsIrJ INPUT=== .z - c LACFCD AND OCEMA PRESSURE FLOM JUNCTION FDRMllLAE USED: DY=~~2*V2-O1~!?1*COSiDELTAl!-Q3+!~3+COSrDELTA3:)- Q~+!~4xCOS<DELTA4!!./I~:Al+A2)*16,1~ UPSTREAII rmwIwS N = .01200 DO1JNSTREA:I MANNINGS N = .01200 LIPSTREAX FRICTIDN SLOPE = ,01328 DOIMIJSTREAtl FRICTIDN SLDPE = .01328 A'JERMED FRIC.TIOI4 SLOPE It4 JUv4C:TIDN ASSUMED AS .01328 ENTRANCE LOSSES = 0.000 JUNCTIOt.1 LOSSES = DY+H!~l-H'~~2+(FHICTION LOSS!+IENTRANCE LOSSES) JUNCTIO'J LOSSES = .272+ 1.689- 1.689+( .053)+! 0.000) = ,345 mrmIOr.; LENGTHCFEET) = 4.00 FRICTION LOSS = .053 NODE 142.10 : HGC= < 270.345>;EGL= < 272,a35i;FLDI,~LINE= < 267.500:> ===========""""""""""""""-~~~~~~~~~"-""""""""""---- - br STREAP1 NODE 140 .00 ELEVATION = 26FJ.70 CALCULATE PRESSURE FLOl,,! FRICTION LOSSES(LACFCD!: PIPE FLO!d = 51 .XI CFS PIPE LEIJGTH = PIPE DlAMETEH = 30.0ci INCHES SF=IQ./K)+r2 = {( 113.86 FEET MA!dt.IJNGS 1.1 = ,01200 'ESURE FLOW PROCESS FROM NODE 142.10 TO NODE 140 .OO IS CODE = 1 ---"----""""~""""""""""""""""""""""""""""" . " 51 .20:)./, 444.352:):)nr2 = .ill32766 ............................................................................ PRESSLIRE FLOlJ PROCESS FROM NODE 140.10 TO NODE 154 ,9U IS CODE = C. UPSTREAII NODE 134.50 ELEVATION = 268.70 " .................................... - c. .-CULATE PRESSURE FLO'A At4(iLE-POitiT LOSSES!LACRD! : PIPE FLOlJ = 36.10 CFS PIPE ANGLE POINT DELTA = 10.00 DEGREES PIPE DIAMETER = 24.00 INCHES PRESSURE FLOW ANGLE-POINT COEFFICIENT KA = ,0300 PRESSURE FLUI,,! UELOCITi' = 11.49 FEET/SEC. i~JELOCiTY HEAD = 2.050 NODE 134.90 : HGL= < 273.251);EGL= < 2?5,3@1);FLOWLINE= < 26E.700) HAPT=KA*IUEL@CITY HEAD) = < .0300)*( 2.C150) = ,062 ....................................... PRESSURE FLO!*I PROCESS FROM NODE 134 -90 TO NODE 135.00 IS CODE = 3 UPSTREAM r4ODE 135, 00 ELEUATI ON = 288.80 CALCLILATE PRESSURE FLOW PIPE-BEND LOSSES(OCEMA) : P I PE FLOI.!.! = 36.10 CFS PIPE LENGTH = 264.47 FEET CENTRAL AI4GLE = 31.400 DEGREES VELOCITY HEAD = 2.050 FLOW VELOCITY = 11.49 FEET PER SECOND BEND COEFFICIENT!KB:~ = ,1477 HB=KBlCVELOCITY HEAD:) = I .148:1+! 2.050:l = ,303 PIPE COr4'JEYANCE FACTOR = 245.076 FRICTION LOSSES = L*SF = ( FRICTION SLOPE(SF) = ,0216977 264.47)*.( .O216?77) = 5.738 PIPE DIAMETER = 24.00 INCHES rlArwINGS 14 = ,012510 PRESSURE FLOW AREA = 3.142 SQUARE FEET NmE 135.00 : HGL= .< 279.292i;EFL= < 281.342i;FLOWLINE= < 288,800) LOST PRESSURE HEAP USING SOFFIT CONTROL = PRESSURE FLOh! ASSUHPTIDN USED TO ADJUST HGL AND EGL 11 -51 NODE 1Z5.00 : HGL= <. 250.8@0?;EtL= < 292,850);FLOWLINE= < 2R8.8C'O) ,- ...................................... ....................................... PRESSURE FLOld PROCESS FROM NODE 135 .00 TO NODE 135.10 IS CODE = 5 UPSTREAM NODE 135.10 ELEVATION = 288.80 CwLCULATE PRESSURE FLOM JUNC.TI ON LOSSES : .-q. DISCHARGE DIAMETER AREA VELOCITY DELTA H'V ...................................... 24.5 24 -00 3.142 7,799 15.800 ,944 2 36.1 24.00 3.142 11.481 " 2 I050 3 0.0 4 0.0 0 .OO 0 .@@!I 0 .000 0 .ooo 0 .00 0 .@OD 0 . 0 0 I1 0 .000 5 11 .6===Q5 EQUALS BASIN INPUT=== - - LACFCD AND OCEMA PRESSURE FLO1.J JLNCTION FORMULAE USED: I'Y=1'Q2r'~~2-Ql*'J1~SaS~~~LTA1)-Q3~~~3ltCOs~aSL~i----------~~- ~ - Q~+Y~+CCIS(DELTA~~~/~~*~~.~) UPSTREAM MANNINGS N = .012@0 DObJNSTREAM FIANI4INGS N = .01200 UPSTREAM FRICTION SLOPE = .@I???? AVERAGED FRI CTIO!.! SLOPE IN JUNCTION ASSUMED AS ,01585 DOIJNSTREAM FRICTION SLOPE = .02170 JUNCTION LENGTH(FEET) = 4.00 ENTRANCE LOSSES = FRICTION LOSS = ,063 JUNCTION LOSSES = DY+Hlil-HV2tCFRIC.TlOt.J LOSS)t<ENTRAtU'CE LOSSES:] .410 NOUE 135.10 : HGL= < 293.55S>;EGL= < 2CS,502>;FLOUL1NE= < 285.800) JUNCTION LOSSES = 2.284+ .944- 2.050tI .063)+< .410! = 1.652 ...................................... PRESSURE FLO!?J PROCESS FROM NODE 135.10 TO NODE 1020 .00 IS CODE = 3 LPSTREAM NODE 1 020.00 ELE'JATION = 306.05 LHLCULATE PRESSURE FLOW PIPE-BEND LOSSES(OCEM4) : PIPE FLOW = PIPE LENGTI? = 24.50 CFS 239.56 FEET PIPE DIAIIETER = 24.00 INCHES CENTRAL ANGLE = 14,500 DEGREES MANNINGS N = .01200 PRESSURE FLOW AREA = 3.142 SQUARE FEET VELOCIT'Y HEAD = ,744 FLOiil '.VELOCITY = 7.80 FEET PER SECOND BEN5 COEFFICIENT!KB! = .lo03 HB=KB*<VELOCITY HEM) = .10Qr*i ,944) = ,095 PIPE CONIIEYANCE FACTOR = 245.076 FRICTION SLOPECSF) = .OD99938 FRICTIOfJ LOSSES = L+SF = ( 235'.56)*': .@0?993P) = 2,394 NODE 1CI20.00 : HGL= .' 2?6.047:);EGL= ( 296.991);FLOWLINE= < 306.050:) " ...................................... PRESSURE FLOiLJ ASSUMPTI@:.! IJSED TO ADJUST HGL AlilD EEL L@ST PRESSURE HEAD USING SOFFIT COI4TROL = 12.00 NODE 1U20.00 : HGL= < 308.050>;EGL= < 308.?94);F:OWLINE= < 30h.050i ...................................... ...................................... PRESSURE FLOIA PROCESS FROV NODE 1020 .00 TO NODE 1020.10 IS CODE = 5 UPSTREAM NODE 1020.10 ELEVATION = 304.05 UPSTREAM MANNINGS bl = .0120@ DOWNSTREAM MANI4INGS N = UPSTREAK FRICTION SLOPE = .00?99 . 0 1200 DOW?dSTREAM FRICTION SLOPE = .00??? AVERAGEP FRICTION SLOPE IN JLbICTION ASSLIHED AS .@@??? YIWTION LENGTH(FEET) = 4.00 FRICTIOiJ LOSS = ,040 JUNCTIO1.1 LOSSES = DYtH'~Il-MJ2tIFRICTIOr.! LOSS:lt<ENTRANCE LOSSES) JIJNCTION LOSSES = 1.887t .?44- .?44t( .040!+! 0.000) = 1.?2? NODE 1020.10 : HGL= < 309,?7?);EGL= < 31@.923);FLOWLINE= < 306.050; rRAt4CE LOSSES = 0.000 ...................................... ....................................... PRESSURE FLO1:I PROCESS FROM NODE 1020.10 TO NODE 101 7 .00 IS CODE = 1 Up,STR€AY ~acnE_1~2~I0---EL.~~~~-~~~~ __-_-___-_ ...................................... CALCULATE PRESSURE FL0l.d FRICTION LOSSES!LACFCD): PIPE FLOW = 24.50 CFS PIPE DIAMETER = 24.00 INCHES PIPE LENGTH = 140.20 FEET PIANNINGS N = .01200 SF=(Q./Kjx+2 = (( 24.50).,'! 245.076))*+2 = .00?5538 HF=L+SF = ( 140.20:1*< .00???38) = 1.401 NODE 1017.00 : HGL= < 311.380);EGL= < 312.324);FLOI,ILIE.iE= < 315.8C.D) PRESSURE FLOW ASSUMF'TICIN USED TO ADJUST HGL AND EGL LOST PRESSURE HEAD USING SOFFIT CONTROL = T-JODE 10!7.0@ : HGL= < 317.86@i;EG;= ( 318.804);FLOWLINE= < 315.860) 6.48 ....................................... """""""""_""""""""""""""""""""""~"""""" ....................................... PRESSURE FLCIW PROCESS FROH NODE 1027.00 TO NODE 1017.10 IS CODE = 5 LlPSTREAFi NODE 1017.10 ELE'JATI nN = 315.86 t - .................................... ,nLCULfiTE PRESSURE FLOlN JUNCTION LOSSES: No. DISCHARGE DIAMETER AREA UELOCIS'; DELTA HV 1 24.5 24.00 3.142 7.799 40.200 .944 2 24.5 24.00 3.142 7.737 " .3 .?44 4 0.0 0 .no 0 .000 0 .no0 0.000 0 . 0 0 .@[I 0 .@DO 0 ,000 0 . 0 0 0 - &l 0.0===05 EQLIALS RciSIN INPUT=== - c LACFCD AN@ UCEMA PRESSURE FLOIM JLINCTIOt-! FOREIIULAE USED: DY=~02*V2-Ql+'~.~l+COS(DELTAl~)-Q3~U3+COS(DELTA3j- 04*V4+COS~DELTA4!!./!~AltA2j+lt.l~ LIPSTREAM ~~NINGs rd = .0120u DOWNSTREAM MANNINES N = .Dl200 UPSTREAI-I FRICTION SLOPE = .@I???? DOIJWTREAM FRICTION SLOPE = .00P?? JUNCTION LENGTH(FEET) = 4.00 ENTRANCE LOSSES = 0.000 FRICTION LOSS = .040 AUERI~GED FRICTION SLOPE IN JurmIord ASSUMED AS .oo?w JUNCTION LOSSES = DYtHVl-H'J2t(FRICTION LOSS!t(ENTRANCE LOSSES) JUNCTION LOSSES = ,446.t .?44- .?44t( .040)t( 0.000) = .466 NODE 1017.10 : HGL= < 318.34t>;EGL= < 31?.2?0>;FLOWLINE= < 315,PLO: -&-:;E PRESSURE FL0l.J FRICTION LOSSESCLACFCD? : PIPE FLOW = 24.56 CFS PIPE DiAI?ETEF: = 24.00 INCHES PIPE LENGTH = 101 -16 FEES MANNINGS N = .01200 """""""""""""""""""""""""""""""""""""== .......................... LlPSTREA!l NODE 10 15.10 ELEVAT1Ot.I = 316.56 CALCULATE PRESSURE FLOW JUNCTION LOSSES: PRESSLIRE FLO1.J PROCESS FROM NODE 1015.00 TO NODE 1015. 10 IS CODE = 5 """""""""""~""""""""""""""""""""""""""- NO. UISCHARCiE DIAMETEE AREA VELOCITY DELTA HV 1 16.2 18.00 1.767 9.167 20.300 1 .305 2 24.5 24.00 3.142 7.799 .944 3 0 4 0 0 .00 0 ,000 0.000 0 ,000 4 0 .0 0 .no 0.000 0 .a00 0 .0@0 5 " - - 8.3===05 EQUALS EhSIrd INPUT=== DY=C02~'~~2-~l*'~.!l+COS(DELTAl~-Q3*~~~*COS(DELTA3:)- LbCFr.D AN0 OCEW PRSSSIJRE .FL~l1;1I~f~l~J-F_D~~I~~~€r~ ________________ ____-__". ~~*~~*COS~@ELTA~:I:I,'II~~~A~:I*~~.~:) LIPSTREAM r.mr.IIrm N = ,01200 DO!+NSTF:EAM MANNINGS N = .@1200 UPSTREAM FRICTIOP.! SLOPE = ,02027 UCfiJNSTREAII FRICT1OP.I SLOPE = .00Y99 A'JERAGED FRIC.TIW! SLOPE IN JUNCTION ASSUMED AS .01513 JUNCTION LENGTHCFEET:] = 4.00 FRICTION LOSS = ,061 ENTRAWE LOSSES = .1 89 - JUNCTION LOSSES = DYtHV1-H1J2t(FR!CT1ON LOSSit(ENTRANCE LOSSES) IXLIDE lD15.10 : HGL= < 320.262>;EGL= < 321.567>;FLOWLINE= < 336.5602 JCTICIN LOSSES = .655+ 1.305- .844t! .061)t( ,189) = 1.265 ....................................... UPSTREA!.: NODE 20 10 .On PRESSIURE FLCU PHOC:ESS FROM NODE 1015.10 TO NODE 2010 .00 IS CODE = 1 ELEVATION = 324.00 CALCULATE PRESSURE FLOIA FRICTION LOSSESCLACFCD): PIPE LENETH = 96.48 FEET rmr4Irm rd = .o1200 SF=IO.,/K)+r2 = (C HF=L*SF = < 16.2@:1/C 113.797):1**2 = ,0202C.5'i NODE 201C,$@ : HGL= { Yc~.217i;EGL= < 323.522?;FLOl~~LINE= ( 324.000:) """"""""""""""""""""""""""""~"""""""""- PIPE FLOh! = 16.20 CFS PIPE DIAtlETER = 18.00 INC.HES 96.48)+( .020265?3 = 1 ,955 2 .> 7, PRESSURE FLOW ASSUMPTION USED TO ADJUST HGL AND EGL LOST PRESSURE HEAD USING SOFFIT CONTROL = 3.28 NODE 2@10.@@ : HGL= < 325,5UO>;EGL= < 326.8052;FLOWL1NE= < 324.0002 I ....................................... ....................................... PRESSURE FLOW PROCESS FROM NODE 201 0 .00 TO NODE 2010.10 IS CODE = 5 UPSTREAN NODE 20 1 0 .1@ ELE1JATIOt4 = 324.00 -"""~""""_"""""""""""""""""~"""""""""""" CALCULATE PRESSURE FLOW JU'QCTI O!4 LOSSES: DISCHARGE DIAMETER AREA VELOCITY DELTA H'J 7.6 2 16.2 18.00 1 .767 eo .2@0 ,458 18.00 5.432 1 .767 9.lt.7 3 0 .O 0 -00 0 .@DO 0 .O00 - 0 .GO@ 1 .305 J 0 . 0 0 .no 0 .@DO 0 . 0 0 0 5 0 .DU@ t..t.===Q5 EQLIOLS &SIP: INPUT=== " - LACFCO AND OCEI:C PRF5?IIRF FI m,, .IIlidTTl nM FnP!.I!II CF IlCFn - ....................................... """""""-~"""""""""""""""""""""""""""~""~ PRESSURE FLOIM PROCESS FROM NODE 2010.10 TO NODE 2008.20 IS CODE = 6 UPSTREAM NODE 2008.20 ELEVATION = 324.00 ....................................... CALCL!LATE PRESSURE FLOI,I ANGLE-POINT LOSSESILACRD:) : PIPE FLOlJ = PTP-1 F PnTNT DFI TA 9.60 CFS PIPE DIAflETEK = 18.00 INCHES PRESSUKE FLOW ANGLE-POINT COEFF1C:IENT KA = .030@ PRESSIJRE FLOW VELOClT'Y = 5.43 FEET./SEC. - - lfi_nF$ VELOCITY HEAD = ,458 NODE 2008.20 : HGL= < 32&.283>;EGL= < 328.742?;FLOI*ILINE= < 324.@00? HAPT=KA+IVELOCITY HEAD;) = i .0350)+! .458! = ,014 "SSLIRE FLO!..d PROLESS FROM NODE 2008.20 TO NODE 2008.00 IS CODE 1 STREArl NCiDE 2008.0C1 ELEiUATION = 327.01 ....................................... PIPE FLOil = CALCULkTE PRESSURE FLOW FRICTIOIJ LOSSES(LACFCD1: PIPE LENGTH = 8L.03 FEET S!==(CfK)**2 = E< HF=L+SF = ( ?.6@)/~ 113.797;)++2 = .no71167 84.03:1+! .0071167:1 = .dl 2 NODE 2008.00 : HGL= < 328,896?;EGL= i 32?.354);FLOWLINE= < 327.010> 9.60 CFS PIPE DIAMETER = 18.00 INCHES rwmIr.!Gs N = .012cto ...................................... ...................................... PRESSLIRE FLOIjJ PROCESS FROM NODE 2008.00 TO NODE 2P08.10 IS CODE = 5 UPSTREA:I NODE 2008. 10 ELEVATION = 327.01 ~~ ~ UPSTREAM FRICTION SLOPE = .00?12 A'JERAGED FRICTION SLOPE IN JUNCTION ASSUMED AS .On712 DOUNSTREAM FRICTION SLOPE = .00712 -"I!NCTlO1.! LENGTHCFEET! = 4.00 FRICTION LOSS = ,028 MANHOLE LOSSES GREATER THAN THOMPSON MOMENTUM LOSSES MOMENTLIM LOSSES = -.000 MANHOLE LOSSES = ,023 ITRWCE LOSSES = 0.000 JUNCTION LOSSES = DYtH'Jl-HtJ2t<FRICTIOR LOSSj+(ENTRANCE LOSSES:) JUNCTION LOSSES = -,000+ ,458- ,458t1 .02R)t( 0.000) = .051 NODE 2008.10 : HGL= < 328.947);EGL= < 329.405);FLOldLINE= < 327.010) ....................................... """""""""_"""""""""""""~""""""""""""""" PRESSllRE FLOi.4 PROCESS FROES NODE 2008.10 TO NODE 2006.00 IS CODE = 3 ?IPSREAI-l NODE 2006.00 ELEVATION = 344.2C CALCULATE PRESSLIRE FLNd PIPE-BEND LOSSES(@CEMH) : PIPE FLOW = 9.60 CFS PIPE DIAMETER = 18.00 INCHES CENTRAL HNGLE = 13.4C0 DEGREES PIPE LENGTH = 20Y.dil FEET MANNlNGS N = .01200 PHESSIJRE FLCU AREA = 1.767 SQUARE FEET FLOI,d 'JELOCITY' = 5.43 FEET PER SECOND VELOCITY HEAD = ,458 BEN[! COEFFICIENTiKP) = .0965 HB=KRI<VELOCITr HEAD) = i .0?6)*,' ,458) = ,044 PIPE C@NVE'fpNCE FACTOR = 113.797 FRICTION SLOPE1SF:I = .0071167 FRICTION LOSSES = LISF = 1 20?.60)+i ,0071167) = 1.492 NODE 2006.00 : HGL= < 330.483);EGL= < 330.941?;FLOWLINE= < 344.200) ....................................... ...................................... ....................................... UPSTREAM NODE 2006.10 PRESSURE FLOI:! PROCESS FROM NODE 2006.00 TO NODE 2006.10 IS CODE = 5 ELEVATION = 344.20 """""_""""""""""""""""""""""""""""""""~ CALCULATE PRESSURE FLOIh! JVNCTION LOSSES: NO. DISCHARGE DIAMETER AREA VELOCITY DELTA 1 9.6 18.00 1 .7t.? H'J 2 5,432 20.000 9 . t 18.00 ,458 3 0.0 i .7t7 5.432 0 .00 0 .000 ,458 4 0.0 0.000 0 .000 0 .00 0. no0 0.000 - 0 .no0 5 0 .@===I25 EQUALS BASIN INPUT=== " - LACFCD AND OCEMA PRESSURE FLOW JUNCTIDN FORMULAE USED: DY~~Q2I'~~2~Ql~'~~l*COS1DELTAl~-Q3I~~3ICOS~@ELTG3~- Q~~Y~*COSIDELTA~))./(~G~+G~~*~~,~:I UPSTREA~I MAwIrm N = .OIZOQ DOWNSTREAM MANNINGS N = .0 1200 UPSTREAM FRICTION SLOPE = .On712 AVERAGED FRICTION SLOPE IN JUNCTION ASSUMED AS ,00712 DOldNSTREAM FRICTION SLOPE = ,00712 JWCTIO1.I LENGTHIFEET) = 4.00 FRICTION LOSS = ,028 .'RANCE LOSSES = 0.000 JUNCTION LOSSES = I.IODE ?0@6.l@ : HGL= < 345.784j;EGL= ( 346.242i;FL@WLINE= < 344.200) JCII4CTION LOSSES = OY+HVl-HVZt(FRICTION LOSS)t<ENTRANCE LOSSES! ,055t .458- .4S8t! .028!+< 0.000) = ,084 . 7 rRESSURE FLOU PROCESS FROfl NOGE 200C,.10 TO NODE 2002.00 IS CODE = 3 UPSTREAM NODE 2002.00 ELEVATION = 360.00 ...................................... CALCULATE PRESSURE FLOW PIPE-EEND LOSSESIOCEMA) : P I P E F L @I>! = P.60 CFS PIPE LENGTH = 145.00 FEET twt~lIrw rd = .01200 CENTRAL ANGLE = 40.000 DEGREES PRESSURE FLO3 AREA = 1.767 SQUARE FEET VELOCIT( HEAD = ,458 FLOW VELOCITY = 5.43 FEET PER SECOND BEND COEFFICIENT!KB:) = ,1667 HB=KB*('UELOCIT'( HEAD:] = I .167:)*( ,458) = .@id PIPE CONVEYANCE FACTOR = 113.797 FRICTION SLOPECSF;) = .0071167 NODE 2002.00 : FGL= < 34&.892>;EGL= < 347.350?;FLOULINE= < 360.000> FRICTION LCISZES = L*SF = I 145.@@:i*I .oo?iit.?) = I .@32 PRESSIURE FLOW ASSUMPTION USED TO ADJUST HGL AND EGL LOST PRESSURE HEAD USING SOFFIT CONTROL = MOUE 2002.00 : HGL= < 14.61 3C.l .500>;EGL= i 361.958);FLOWLIHE= < 360.000) PIPE DIAMETER = 18.00 INCHES ...................................... PRESSURE PIPE-FLOIJ HYDRAULICS COMPUTER PROGRAM PACKAGE - <Reference: LACFD,LACRD,& OCEMA HYDRAULICS CRITERION) ............................................................................ <(!(((({;;((({({(((((((((((~(((((!({(())?)?))?))?)))}~??)))?))?))}:)???)))))) <C! Copyright 1982 Advanced Engineering Software [AESI Especially prepared for: EIANITOU ENGINEERING COMPANY (((((<<~((((((<<(((((({(((((((((!{({(<}))):):)?)?:)?)):)??))??):))))))?)):):):)j))):~ ............................................................................ NOTE: STEADY FLOlnI HYDRAULIC HEAD-LOSS CDMPUTATIOI4S BASED OF4 THE tlOST CONSERVATIVE FORMULAE FROM THE CURRENT LACRD,LACFCD, AI4D OCEMA DESI GrJ rwuALS. NODE NUMBER = 61S.00 DOWNSTREAM PRESSURE PIPE FL0.N C.ONTROL DATA: ASSUMED 0OWNSTREAM CONTROL HGL = 389.000 PIPE DIAMETER< ItKH) = 30 .00 PIPE FLOW<CFS! = 37 * 60 FLOLILINE ELEVATION 366.50 """"""""""""""""""""""""""""""""~""--"--- """""_""""""""""""""" .............................................................. PRESSURE FLOW PROCESS FROM NODE 615 .00 TO NODE 610 .00 IS CODE = 1 UPSTREAM NODE 61 0. 00 ELEVATION = 391 .60 CALCULATE PRESSURE FLOlnl FRICTION LOSSES<LGCFCD) : PIPE LENGTH = 100.00 FEET rww Irm t4 = . o 1200 E:F=(Q,/K)**2 = I( 37.60>/! 444.352))**2 = ,0071601 HF=L*SF = I 100.@0:)*( ,0071601) = * 71 6 NODE 610.00 : HGL= < 38?.716>;EGL= < 3?@.627>;FLOWLINE= < 3?1.800> PRESSURE FLOlni ASSUMPTION USED TO ADJUST HGL AND EGL LOST PRESSLIRE HEAD USING SOFFIT CONTRDL = 4.58 """"""""~""""""""""""""""""""""""""""--- PIPE FLOI:.! = 37.60 CFS PIPE DIAMETER = 30.00 INCHES """"_"""""""""""""""""""""""""""""""""~ NODE 610.00 : HGL= < 394.300>;EGL= < 395,21l);FLOl~lLINE= < 391.800> ...................................... ....................................... PRESSLIRE FLOW PROCESS FROM NODE 610.00 TO NODE 609.00 IS CODE = 5 IIPSTREAH NODE 609.00 ELEVATIO1.l = 371 .W ,- 'ILATE PRESSURE FLOI,J JLINCTION LOSSES: "_""""""""""""""""""""""""""""""""""""~ DISCHfiRGE DIAMETER AREA LJELOCITU DELTA I-N) - 6.9 WI n 1.7~-_38~EI"-~,cLoa----~Q----- = 37.6 30 .00 4 .YO9 7.660 " .Pll 3 4 0.0 0 .00 0.000 0 .0 0 .00 0 ,000 0.000 ii .000 ,000 0 .000 J 30 .8===~5 ERLIALS mx1r.I INPUT=== - - c LACFCD &NE OCEMA PRESSURE FLOW JUtKTION FORMULAE USE@: DY=(R~~*~.~J~-~~*~J~~COSI[~ELTA~:I-~~*'.~~~C@S~[~ELTA'~:~- ~4~V4*COS~~@ELTA4:)~/~~Altk2:~*16.l! UPSTR.EAM MarmIrm r4 = .o1200 DOWNSTREAM MANNINGS N = .01200 A'JERAGED FRICTION SLOPE IN JLINCTION ASSUMED AS ,00537 DOWNSTREAM FRICTION SLOPE = ,00716 JUNCTION LENGTH':FEET:l = 4.00 FR1CTIOr.I LOSS = ,021 ENTRkNCE LOSSES = ,182 JCllJCT I ON LOSSES = 2.436t .230- ,911tI .021!t( .182:l = 1.959 NODE 609.00 : HGL= < 396.940: ;EGL= < 39i.l70>;FLOWLINE= < 391 UPSTREAl.1 FRICT1OI.I SLOPE = .00357 JUNCTIOI4 LOSSES nY+H?Jl-H'J2tIFRICTI01.1 LOSS)+(ENTRANCE LOSSES) ,/- -.SURE FLOII' F'ROCESE: FROM b!ODE 609.00 TO NODE 605.00 IS CODE = 1 !EAH NODE 605.00 ELEVATION = 395.56 .. "~"""""""""""""""""""""""""""""""""- LHLCULATE PRESSURE FLOlJ FRICTION LOSSES!LACFCD) : PI PE FLOW = 6.80 CFS PIPE @IAMETER = 18.00 INCHES PIPE LENGTH = 81.72 FEET HF=L*SF = < 8!.72!*< .0035707) = NODE 605.00 : HGL= < 3?7.232i;EGL= < 39?.462:>;FL@WLINE= < 395.560; .292 MAN~~INGS N = . 0 1 200 SF=iQ./K)rx2 = ((( 6.80)/< 113.797!!**2 = .003570i