HomeMy WebLinkAbout1891 RUTHERFORD RD; ; AS990032; Permit5/18/22, 10:39 AM
Job Address:
Permit Type:
Parcel No:
Lot#:
Reference No.:
PC#:
Project Title:
Applicant:
Fees($)
544
AS990032 Permit Data
City of Carlsbad
Sprinkler Permit
Permit No: AS990032
1891 RUTHERFORD
Status: ISSUED
RD
SPRINK Applied 7/16/1999
2121203600 Approved:
0
Issued:
Inspector:
ISIS PHARMACEUTICALS
Add'I Fees ($)
0
Owner:
DIVERSIFIED CARLSBAD 47&48 LL C
C/O WILLIAM TSCHANTZ
1770 GILLESPIE WAY #101
EL CAJON CA
Total($) Balance($)
544 0
1 /1
Carlsbad Fire Department AS C\~0032 990203
2560 Orion Way
Carlsbad, CA 92008
Fire Prevention
(760) 931-2121
Plan Review Requirements Category: Auto. Sprinkler, OH
Reviewed by: Date of Report: 07/27/1999 ------------
Name: Action Fire Systems
Address: 9185 Harness St
City, State: Spring Valley CA 91977
Plan Checker: Job #: 990203
Job Name: Carlsbad Research Bldg #: CB991613 ------------------
Job Address: 1891 Rutherford Rd Ste. or Bldg. No.
~ Approved
D Approved
Subject to
D Incomplete
Review
FD Job#
The item you have submitted for review has been approved. The approval is
based on plans, information and / or specifications provided in your submittal;
therefore any changes to these items after this date, including field
modifications, must be reviewed by this office to insure continued conformance
with applicable codes and standards. Please review carefully all comments
attached as failure to comply with instructions in this report can result in
suspen_sion of permit to construct or install improvements.
The item you have submitted for review has been approved subject to the
attached conditions. The approval is based on plans, information and/or
specifications provided in your submittal. Please review carefully all comments
attached, as failure to comply with instructions in this report can result in
suspension of permit to construct or install improvements. Please resubmit to
this office the necessary plans and / or specifications required to indicate
compliance with applicable codes and standards.
The item you have submitted for review is incomplete. At this time, this office
cannot adequately conduct a review to determine compliance with the
applicable codes and / or standards. Please review carefully all comments
attached. Please resubmit the necessary plans and / or specifications to this
office for review and approval.
1st
990203
2nd
FD File#
3rd Other Agency ID
.. ASC,C\0052. r
ACTION
·FIRE SYSTEMS
1
----------------------r.-1R :IRR1RO ;,..· ----------------------HYDn l\U LIC _DE SIGN lNf-ORMATION SHEET
MAME. /:}/..!] /7#A,£M,4c? .i!Cl_?:/C!/lC..S La7_4,£:, OATE_7-.QL.r? -----
l.OCATION~~L_~z:e./lf£e0£C> ,,££} • -~A/??-S4$AP~ C7 &_, ·------~
BUJLOING • G Q.. 7" 4$ SYSTEM, NQ _________ _
CONlRACTOA~ e,U~/~ <--' c'!crJ 6'.-Z;__, ~ C'. ~---<XHffRAci No._fl~'8-~---
CALCULA TED BY D__{J_p,-J J .:1 ~_o,.:)~flL-t/£_,? ___ r _____________ DAAWING N0 .. -~2_,_, _______ _
CONSH\l..'CTION: fX!_ COMBIJS llOl.E ( J NON-COMBU5TIBLf. CEILING HEIGHT._..,.._23'_9 ,, _ __fT.
OCCllf'fd,JC'Y •••-••~E...c.L.c? ~-L.L. .. r-~ /...rH.__ A) ,:E&t..J 1),,411; Z:.~Add..t4~---
ORD. HAZ. GP.
FIGURE r-
( J 1 ) 2 l J J ) EX. HAZ.
CURV-· ____ _
C:ALCULAT10N
SUMMAnY 1
GPr,1 REOUIRED_41.4 .... • ,._• _j __
"C'' FACTOR USED:
PSI FIEOUIR(D __ _!]_ 7,_4-~_ AT BASE Of R1m:n
OVF..RHEAO _ _Lg~ UNDERGROUND. /5()
>-_J
c ..
0.. ::-> V,
cc • UJ 1-<t ;:.
UJ
C) <t a:
0 ln
)-t
0 0 :E ... 0 u
WATE A FLOW TEST I
DA TE & TIM( . s-L!L9'<:!!'> ____ _
STA TIC PSI J:ZO
RESI.DUAL PSI // 5' ____ _
GPM FLOWING __ / __ 5_='__,0 ___ _
ELEVATION
PUMP DAB
RATED ~PACITY ·-
Al PSI
ELEVATION •.
toe Ar 10,-1 __ _g_f/_ -r /-r: ~/?..~ ~?_Q_~O r -----~--·--
sou R cE OF INFORMATION~_£. S, J C:, /\A, W_i_f} , _ _ft_ __ ~_L) ____________ _
~ l)
c{ .I a:
--------------CLASS _________ LOCATION -------.-c:..-----
-------------ARE A AISLE WIDTH~----------
) SINGLE ROW
) DOUBLE HOW
) MULTIPLE ROW
-----"' PALLETIZf.D _____ ~.,,.. --------"
J E~CAf>SULATt:D
J NON•
ENCAPSULATED
Dc.7\te: 11/01/91
JOB TITLE: ISIS PHARMACEUTICALS
WATER SUPPLY DATA
SOURCE
NODE
Tf-lG
STt:4T IC
PHEBS.
(Vi:H )
HESI D.
Pl~E~"3S. l}.f
( Pf3 I )
FLDl,,J (.WnlL.
PF!E~:3S. t]J
( Gf-1M) <Pbl )
TDTf.4L.
DEMf.~l'JD
<GPM)
Pag£:: 1
C: \BL~2
HEQ'D
PHESS.
<PSI)
Ul * 108.0 ~103.~::i 1530 .. 0 .1.07.4 5;::'.4 .2
--i(-,R£pcle€0 6v /Odj'tr rtJ/Z-evs#ro~
AGGREGATE FLOW ANALYSIS:
TOTAL FLOW AT SOURCE
TOTAL HOSE STREAM ALLOWANCE AT SOURCE
OTHER HOSE STREAM ALLOWANCES
TDH~L DISCHr~RC::iE FF<OM ~':\CTI VE SPRIN~{LERS
NODE ANALYSIS DATA
NODE
l IZI 1
102
11213
104
105
1 tZtt-:,
1 tZl7
108
10'::)
110
111
1 u~
113
114
11 ~~-i
116
l.17
118
119
120
121
122
123
12Lt
12~i
126
127
128
129
130
131
13i:?:'.
1 7··;-.;:,,..,
134
TAG ELEVATION
<FT>
28.8
28.8
28.8
28.8
28.8
i:'.~8. 8
28.8
28.8
2B.8
i::'.8. 8
28.8
28.8
2B. B
28.8
28.8
28.8
28.8
28.8
28.8
28.8
28.8
28.8
28.8
28.B
28.8
i::'.B. 8
28.8
28.8
28.8
28.8
28.8
28.8
28.a
28.8
NODE TYPE PHESSURE
(PSI)
83.2
B3.3
B3. Lt
83.4
83.5
83.6
83.6
B3.7
83.8
83. 1
83.2
8~?:;. L►
f)3. L~
83.6
83.7
83 .. 7
83. 1
83. i.~
83 .. 4
B3. Lt
83.5
83.6
B3.7
83.7
83.3
83.3
83.4
83.5
83.6
83.6
83.7
5;:::4. 2 GPM
:-jQL Q) GPM
50.0 GPM
Lt24 .. 2 GPM
DI SCHf.:1 F<GE
<GPM)
SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2
JOB TITLE: ISIS PHARMACEUTICALS
~ODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE
(FT) <PSI) <GPM)
151 28. 8 01 •• 2
15~~ i='.8. a EV+. ;:::
15~3 28. 8 8'+ • .....
154 ;:::8. 8 8-4-.. ? .....
1 c.· t::· ...J .. J i.:~8. 8 8.1i • ~;
156 ;;::8. 8 84 .. L•
1 r::·-, Ji i.::'.8 . 8 84. 4
15B i:::8 .. 8 84. 4
1~_;9 28. 8 81+. L•
160 i::'.8. B 84. 2
161 28. 8 a.1. ... 2
162 28. 8 84. -... --~
163 28. 8 BL + .. -. ~
164 28. 8 84. L•
165 28. B 8L1-. i►
166 i::'.8. 8 84. 4
167 f:B .. B 81+. c:· ,._c
168 c~H. 8 84. 5
1("\g 28. 8 83. ( ....
170 28. 8 G --. d~. 6
:1.71 28. 8 83. 7
1 7,~~ i:~8. B 83. f3
173 28. 8 83. 9
l.74 28. 8 83. 9
175 28. 8 BL ... 0
176 ;;~8. 8 B'+. 1
177 ;:::B. 8 81+. 2
178 28. 8 B3. 7
179 28. 8 83.8
180 28. 8 83.8
181 ;.:.::8. 8 83. 9
182 28. 8 84.0
183 28. 8 8L►• 1
184 28. 8 8L1-. 2
201 28. 8 82.0
20,:: 28. B 82.0
203 28. 8 B2. 0
cJZl4 28. 8 82 .. 2
i.~05 28. 8 82. 2
206 28. 8 82 .. 2
207 28. 8 82 .. 1
208 ;;::8. 8 82. 1
209 i::'.8. 8 82. 1
301 11. 2 L•7 • ')
30i.:~ 11. 2 47. Cj
303 11. 2 47.·➔
30L► 11. 2 L1-9 • c:-,._I
305 11. i::: 49. 1::.-..J
306 11. .-, 1.-::. Lt-9 • 5
307 11. t::-... J 50. C)
308 11. 5 ~51Zt. 9
309 11. 5 ~50 . 9
310 11. i:-.::, 5lt). 9
311 11. 3 ~.52. 4
\
SPFH N•<L.Ef< SYSTEM HYDRAUL. IC ANAL YSI B Page 3
JOB TITLE: ISIS PHARMACEUTICALS
~ODE TAG ELEVATION NODE TYPE PRESSURE DISCHARGE
<FT) <PSI> (GPM)
312 11. 3 ::c:_::;. 8
313 11. 2 r··r-;.);:'J,. r.::--..J
31 Lt 11. 2 ~5~5. r.:· ._(
~)0 10.6 48. 2
::j 1 10.6 it-9. 7
~)i::'. 10.6 ~:il. ..... ~
c:· ..... J~ 10. ( ... 52. B
~S4 10.6 54. 1
~;5 10. ( ... r::-c::· ,_•~·. 7
~ .. ff."\ 10.6 68 .. a
57 10.6 BL 2
1Q 9. 0 i:~7 . B i::'.9 .. IZI
J.R 11. ~; 28. 9
2Q 9.0 29. 1 29.7
2R 11. 5 3tt.'t. c::· ...}
3Q ':).0 2L,-. 2 27. 1
3R 11. 5 25. 1
Lt-Q 9. 0 I-<= 5. 5tZt ~~5. 6 27.8
4R 11. 5 26. Lt
~jQ 9.0 I-<= 5. 50 35. 121 32.5
5R 11. 5 2;6. 2
GQ 9.0 16. 7
6R 11. 5 17. 1
7Q <). Ii.) I-<= 5 .. 50 1 7. -::, '·-2i~. 8
7R 11. 5 18. 0
8Q 9.0 I-<= 5. 50 20. 7
8R 11. 5 i::'. 1 • .L.
C)Q '}. Qt 16. B
9R 11. 5 16. 8
10Q 9.0 !-(,= 5. 50 17. i:::--..J 23.0
10R J.1. 5 18. 1
11Q 9. 0 i::'.0. 9 25. 1
11 H 11. 5 f:1. 6
li::'.Q 9.0 I·<= 5. 50 35. 2
l c~F< 11. 5 36. 5
13Q 9.0 17. 1
13H 11. 5 1 7. 1
ll,-Q 9.0 . I-<= 5. 50 lB .. 0 23.3
14R 11. ~-i 18. 5
15Q 9.0 I-<== 5. 50 21. c:-._(
15R 11. 5 22. Q.'t
16Q 9.0 I-<= 5. 50 35. 7
16R 11. 5 -:i_;7. 2
L,-5 10.6 3•:,. 6
4& 10.6 39. 8
47 10.6 40. 0
'+8 10. 6 '+0. Lt
'+9 10.6 41. i:°::
1 26.0 83. Lt-
2 26.0 83. -7
I _/
3 26.0 8(--.. 0
4 26.0 83. 4
5 26.121 86. 0
G 26.0 a ·--,.:~. 4
SPRINKLER SYSTEM HYDRAULIC ANALYSIS
JOB TITLE: ISIS PHARMACEUTICALS
~ODE TAG ELEVATION NODE TYPE
<FT>
7 26. 0
B c=:6. 0
9 26. 0
10 26 . IZl
1 1 26. Q)
1 .-, i::. 26. IZl
13 f:6. 0
14 26. IZl
14A 26. 0
15 26. 0
16 26. 0
17 26. 0
18 26. 0
19 i::'.6. 0
2121 26. 0
21 26. 0
f:2 2('\. 0
22A 28. 8
23 26. 0
24 i.~6. 0
24(-:'\ 28. 8
. -,c::-C..J 2(, • 0
i::'.6 26. 0
27 26. 0
28 26. 0
29 26. 0
3121 26. 0
30A 28. B
31 2('\. Q)
TOH 25. i:::-.J
BOR 0. 5 HOSE ST~<EAM
U5 --3. IZl
U4 ·=· '-. 0
U3 f:. tZI
Ui.~ -3. 0
Ul -3. 0 SOURCE
PRESSURE DISCHARGE
(Vi'3 I) <GPM>
86.0
83.4
86. fl)
83 .. 3
83. 1 ---
B5.9
83. 1
H5.9
83.2
85.9
83.2
85.9
82. l
85.9
(:33 . 2
82.2
83.8
8.lt-. 1
85 . .li-
85. 8
8~5 • l)
83. f'.
8i::'.. 0
86.0
86.4
97 • .lt-
98. 9
97.3
102.3
1'l.V1-. 6
10.lt-. 7
50.0
.lt-74. 2
Page 4
SP H I N ~~LE f< £NSTEM HYDHAULIC AN~lLYBIS Page 5
JOB TITLE: ISIS PHARMf'.'.~CEUT I CALS
PIPE D~lTA
PIPE T~~G G! <GPM) DIA<IN) LENGTH PRESS.
END ELEV. NOZ. PT DISC. t)EL <FPS) HW(C) <FT> SUM.
NODES <FT) (K) <PSI> <GPM) F.Ln/FT <PSI)
Pipe: 1 -·-32. ':l 2 .. 203 PL 20 .. 33 PF 0 .. 3
l f~6. 0 0.0 83. i► 12). 12) 2.8 120 FTG T2L PE 0. 0
2 i::'.6. 0 0.0 f33 .. 7 It). 0 0.009 TL 36.33 PV 0 .. :l
Pipe: 2 -32.9 2.203 PL 70.00 PF 0. 7
-:::, '--f~6. 0 0.0 B3.7 0 .. 0 2.8 li::'.0 FTG T PE 1. i:~
101 28 .. B 0.0 8~;. c~ 0 .. 12t 0.009 TL 80. 0'21 PV 0. 1
Pipe: ·-;-,..> -·-32. 9 2.203 PL 8. tZt0 PF 0. 1
101 28.8 0.0 83.2 0.0 2 .. 8 121li FTG PE 0.0
102 28 .. 8 0.0 f.33 .. 3 0 .. 0 0 .. 009 TL 8 .. 00 p1...,1 0. 1
Pipe: LJ, --2;2. 9 2. 20~; PL 8. 0ft) PF 0. 1
10i::'. 28.8 0. 0 C . ..,, "'"\ '-:L.:,. _:, 0.0 2.8 li::'.0 FTG PE ,~., l{J
103 28.8 0. 0 83. L► II..~. 0 0.009 TL 8.00 PV 0. 1
Pipe: 5 ·-32. 9 i~ .. C~03 PL 8.00 PF 0. 1
103 28.8 0.0 83. L► It). 0 2.8 120 FTG PE 0.0
104 ~::8. 8 0.0 83.4 0.0 0.009 TL 8.00 Pl) 0. 1
Pipe: 6 -32.9 2.203 PL 8. 1£'0 PF 0. 1
104 28.8 0.0 83.4 0.0 2.8 120 FTG PE 0. 0
105 28.8 0.0 83.5 0. 0 0.009 TL 8. '210 PV 0. 1
Pipe: 7 --32. 9 2 .. 203 PL 8.00 PF 0. 1
105 28.8 fl,. fl) 83.5 fl). 0 2.B 120 FTG PE 0.0
10("\ 28.8 0.0 83.6 0 .. 0 0.009 TL 8.00 PV 0. 1
Pipe: 8 -32.9 2.203 PL 8.00 PF 0. 1
1 tZH~ 28.8 0.0 83.6 0.0 2.8 120 FTG PE 0.0
107 ;.:.::a. B 0.0 83.6 0. ll.i 0. 01219 TL 8.00 p1...,1 0. 1
Pipe: ':) ---:3i?::. 9 i::'. .. 203 PL 8. 00 PF 0. 1
107 28.8 0.0 83.6 0. 0 2.8 120 FTG PE 121. 0
108 ~~8. a 0.0 l:33.7 0. 0 0.009 TL 8.IZIIZI PV 0. 1
Pipe: 10 -32.9 2. 20~; PL 8. 0121 PF 0. 1
11218 28.8 0.0 83.7 tZt. 0 2.8 120 FTG PE 0.121
109 28.8 0.0 83.8 12.,. IL' 0.009 TL 8. 0121 PV 0. 1
Pipe: 11 --32. 9 2.203 PL 87.00 PF 0.9
109 28.8 121. tZI 83.8 0. Qt 2.8 120 FTG 2T PE 1 .-. • C.
3 26 .. 0 0.0 B6. 0 0.121 0.009 TL 107.00 PV 0. 1
Pipe: 1 .-, a::. -34.121 2.21213 PL 80. 121121 PF 0.9
4 26.0 0.0 83.4 0.0 2. '-) li:::0 FTG 2T PE 1 -::, • I....
110 28.8 0.0 82;. 1 fl'. tZI 0.009 TL 100. 00 PV 0. 1
Pipe: 1 ---... ~ -~3L~ • 0 2. 212,~3 PL B.00 PF 0. 1
110 f~B. 8 121. 0 83. 1 0.0 2.9 120 FTG PE 0.0
111 28.8 IZI. IZt 83. j~ 0. 0 0.009 TL B.00 PV 0. 1
SPRIN~(LEH SYSTEM HYDRAULIC ANALYSIS Page ("\
JOB TITLE: IBIS PHARMACEUT I Cr::'.\Lf:3
PIPE Df-Hf.'.l (cont'd)
PIPE TA{3 Q(GPM) DIA<IN> LENGTH PF<ESS.
END ELE\.1• NOZ. PT DISC. VEL<FPB) HW(C) <FT) SUM.
NODES <FT> < K) <PFH) <GPM) F.L./FT <PSI)
Pipe: 14 --34. 0 2. i::'.03 PL 8.00 PF 0. 1
11.1 28.8 l{.1. 0 83. i.::'. l{.1. 0 i::'.. 9 121l1 FTG PE 0. 0
112 28.8 0.0 B3.3 c~. 0 0. 0C~9 TL 8 .. 00 PV 121. 1
Pipe: 15 -.311-. e, i:::" i:~fl)~; PL 8.00 PF t21. 1
112 2f3. 8 0 .. 0 83.3 0a 0 2.'➔ 120 FTG PE 0. It)
113 28.8 0.0 83.4 0" 0 0.009 TL 8. 0,1 PV 0. l
Pipe: 16 --3Lt-. tZI 2.203 PL. 8.00 PF 0. 1
113 28.8 0.0 82:;n lt-0. 121 2.9 12tt) FTG PE 0.0
114 28.8 0.0 83.4 0.0 0.009 TL 8 .00 PV 0. 1
Pipe: 17 -34.0 2. 20~; PL 8. 1210 PF 0. 1
114 28.8 0.0 83.4 0. 121 2 .. 9 120 FTG PE 0.0
115 28.8 0.0 82:;. 5 0. 0 0.009 TL 8.00 PV 121. 1
Pipe: 18 -3Lt-. 0 2. i.~03 PL 8.00 PF 0. 1
115 i.:'.8. 8 0.0 B3.5 flt. QI i::'.. C) L:::0 FTG PE 0.0
116 28.8 0.0 83.6 0.0 0.009 TL 8.00 PV 0. 1
Pipe: 19 -~A. 0 2. 21l'l3 PL 8.00 PF 0. 1
116 ~::8. 8 0. 0 83.6 0.0 ;~. 9 li~0 FTG PE 0.0
117 28.8 0.0 83.7 ll'l. 0 0.009 TL 8.00 PV 0. 1
Pipe: 20 ·-3Lt-. 0 2.203 PL 8.00 PF 0. 1
117 28.8 0. e, 83.7 0.0 2.9 120 FTG PE 0.0
1 H~ 2B.8 0.0 83.7 0. 121 0.009 TL 8.00 PV 0. 1
Pipe: 21 -3'+. ll'l 2. 20~; PL 87.00 PF 1.0
118 28.8 0.0 83.7 0.0 2.9 120 FTG 2T PE 1..2
5 26.0 0. 0 86.0 0.0 0.009 TL 107.00 PV 0. l
Pipe: 22 ·--3Lt-. 1 2.203 PL 80. 00 PF IZt.9
6 26.0 0.0 83.4 121.0 2.9 120 FTG 2T PE 1 .-, • C.
119 28.8 0.0 83. 1 0.0 0.009 TL 100.00 P\.' 0. 1
Pipe: 23 -34 . 1 2.203 PL 8.00 PF 0. 1
119 28.8 0.0 fB. 1 0.0 ;=.:. 9 li::'.0 FTG PE 0.0
120 28.8 0. lt°:1 B3.2 0.0 ll.'l. 009 TL 8.00 PV 0. 1
Pipe: 2l• -3-4-. 1 2.203 PL 8.00 PF 0. 1
120 i.::'.8. 8 0. 0 83. 2 0.0 2.9 120 FTG PE 0.0
121 28.8 0.0 83.3 0.0 0.009 TL 8.00 PV 0. 1
Pipe: .-·,c:· C . ...J -311-. 1 2.203 PL 8.00 PF 0. 1
121 28.8 0.0 83.3 0. 0 2.9 120 FTG PE 0.0
122 28.8 0.0 8~;. Lt-0. ll.'l 0.009 TL 8.00 PV 0. 1
Pipe: 26 -3L1-. 1 2.203 PL 8.00 PF 0. 1 1 .-,.-·, cc. 28.8 ll.'l. 0 82;. L• 0.0 ·2. 9 120 FTG PE 0.0
123 28.8 0.0 83. '+ 0.0 0.009 TL B.00 PV 0. 1
SP RI NI·< LE f< SYSTEM HYDH~~UL IC ANALYSIS Page 7
JOB TITLE: ISIS PHARMACEUTICALB
PIPE DATA (cont'd)
PIPE H~G Q<GPM) DIA<IN) LENGTH PRESS.
END ELEV. NOZ. PT DISC. l.,'EL <FPS) HW<C> <FT> SUM.
NODES <FT) 00 (PSI> <GPM> F. L. /FT <PSI)
Pipe: 27 ··-3Lt-• 1 2.203 PL 8. tZltZI PF 0. 1 u·::3 28 .. 8 0.0 B3 • .1.,. If). 0 2.9 120 FTG PE 0.0
12L► 20 .. 8 0. tZI H3 .. ~S 0. ,~ 0. 00') TL 8. 00 PV ~:). 1
Pipe: 28 --3.1.t-. 1 2 .203 PL 8.00 PF 0. 1
124 28.B 0.0 83.5 0. ILi 2.9 120 FTG PE 0. tZt
1i::'.~i 28.B 0. It.~ 83.6 0. ,;,~ I,~. 009 TL 8. 00 PV 0. l
Pipe: i:~9 ·--3Lt-. l i~. 203 PL 8.00 PF 0. 1
125 2a. ·a 0.0 83.6 it.i .. 0 2.9 :1.20 FTG PE 0.0
126 28.8 0.0 83.7 0.0 0.009 TL 8.00 PV tZI. 1
Pipe: 30 -3.lt-. 1 2. 203 PL 8.00 PF 12:1. 1
126 28.8 0.0 8~3. 7 0.0 2. •=) 120 FTG PE 0.0
127 28.8 0.0 83.7 It). 0 tZl.009 TL 8.00 PV tZI. 1
Pipe: 31 ·--3Lt-• 1 i::'.. 203 PL 87.00 PF 1.0
127 28.8 0.0 83.7 0.0 2.9 ii:::0 FTG 2T PE 1 .-, . ,::.
7 26. tZt 0.0 B6.0 0. ':) 0.009 TL 107.00 PV 0. 1
Pipe: 2;2 --3.1.•. 4 2.203 PL 96. ll.'0 PF 1. 1
8 26.0 0.0 83.4 0.0 2. 9 120 FTG 2T PE 1. f~
128 28.8 0.0 B3.3 it.i. 0 0.010 TL 116.00 PV 0. 1
Pipe: 33 ---. , ---~.q. 4 2.203 PL 8. 1210 PF 0. 1
128 28.8 0.0 82:;. :~; 0.0 2.9 120 FTG PE 0.0
129 28.8 0.0 8~3. 3 tZlntZI 0.010 TL 8.00 PV 0. 1
Pipe: 34 -3Lt-. 4 i~. 203 PL 8.00 PF 0. 1
129 2B.8 0.0 a-· ·--\.J ■ ,_, 0.0 2 .9 120 FTG PE 0. l[.'I
130 i::8 .. 8 121. It) 83. L• ,~,. ,z, 0. 01 It.~ TL 8.00 PV 0. 1
Pipe: 3~:j -34.4 2.203 PL 8.00 PF 121. 1
130 28.8 0.0 B3. Lt-12\. lli 2.9 120 FTG PE 0.0
131 ~::8. B 0. tZI 83. ~) tZI. 0 0. 010 TL 8.00 PV 0. 1
Pipe: 36 -31►• 4 i:!.. 203 PL 8.00 PF 0. 1
131 28.8 0.0 83.5 0.0 2.9 12121 FTG PE 0. 0
132 28.8 0.0 83.6 121.0 0.010 TL 8.00 P\...l 0. 1
Pipe: 37 ---3L~. 4 2.203 PL 8.00 PF 0. 1
132 28.8 0.0 83.6 it.1. 0 2.9 120 FTG PE 0.0
133 28.8 0.0 83.6 0.0 0. 010 TL 8.00 PV tZI. 1
Pipe: 38 -3.l•· '-• 2. 202; PL 8.00 PF 0. 1
133 i::'.8. 8 0.0 83.6 0.0 2.9 120 FTG PE 0. IZt
134 28.8 0.0 83.7 0. ,21 0.010 TL 8.00 PV 0. 1
Pipe: 39 -34.4 2.203 PL 87.00 PF 1.121
134 28.8 0.0 83.7 0. t2t 2.9 120 FTG 2T PE 1.2
<) 26.0 0.0 86.0 0.0 tZl.010 TL 107.00 PV 0. 1
~,PR I N~<LEH SYSTEM HYDRAULIC ANf-lLYS IS Page 8
JOB TITLE: ISIS PHAF<Mf~CEUT I CALS
PIPE DATA (cont'd)
PIPE Tf~lG Q(GPM) DIA<IN) LENGTH PREE~S.
END ELEt,,1• NOZ. PT DISC .. VEL<FPB> HW(C) <FT> SUM.
NODES <FT> 00 (PBI > WPM> F" L. /FT <PSI>
Pipe: 40 --3.l►,, a 2. 21213 PL 23f.. 00 PF ~::'. .. 7
10 i.:'.6. 0 0. Q.1 [\2_;. -~·· 0n lt?J i:~ .. 9 12ft) FTG 4T PE It). 0 \oJ
11 26. IZI 0.0 B6.0 li.L 0 0.010 TL 271.00 PV 0. 1
Pipe: '+ 1 -·35 .. ,21 2. 202; PL 231. 00 PF 2.7
12 26.0 0 .. 0 l) ·-. ..._ \. ,.-:, .. '9~ ti..'l.0 i~~-9 120 FTG 4T PE 0. ti.)
13 26.0 0.0 85.9 ti.). 0 0.010 TL 271. 00 PV 0. 1
Pipe: 42 -35.7 2.203 PL 231.0121 PF i:::. a
14 26.0 0.0 8:3. 1 0.0 3.0 121l1 FTG 4T PE 0.0
15 26.0 0.0 B5.9 0. i;~ 0. 010 TL 271. 1210 PV 0. 1
Pipe: i~3 -·36. 0 ;~. i~0~; PL i='.31. IZl!i.1 PF 2 .. 8
16 i::'.6. 0 0. 0 8-;-...., . 1 0.0 3.0 120 FTG 4T PE 0.0
17 f~6. 0 0. e, 85.9 0. ll1 0. ll.110 TL 271.. 00 PV 0. 1
Pipe: 44 --35. 4 2.203 PL 231. 00 PF i::'.. 7
18 26.0 0.0 83. i.::'. 0 .. 0 3.0 1212.1 FTG "►T PE 0.0
19 i::'.f~. tZl 0. "?.'I H5.9 0. 0 0. 0 1 Qt TL 271. 00 PV 121 .. 1
Pipe: "►~i --35 .. 1 2. ;;:02; PL 152.33 PF 1.7
;:.=~0 2f,. 0 0.0 B3.2 0. Ii) 3. 0 1~::0 FTG ;:;:T PE 1. 2
178 28.8 0.0 83.7 e,. 12.'I 0. ll11 ll1 TL 172.33 PV ll.1. 1
Pipe: 46 -35. 1 2.203 PL 8.00 PF 0. 1
178 f:8. 8 0.0 83.7 ll.1. 0 3. ll.1 120 FTG PE 0.0
179 28.8 0.0 83.B tZl.0 0.010 TL 8.00 Pl..' 0. 1
Pipe: 47 ---c:· -,.!,-...J. 1 c:. 20~; PL 8.00 PF 0. 1
179 28.8 0.0 83.8 0.0 3. tZI 120 FTG PE tZl.0
18121 28.B 0.0 83.B 0.0 0.010 TL 8.00 PV 0. 1
Pipe: 48 --2;5 . 1 2.203 PL B. 00 PF tZI. 1
180 28.8 0.0 83.8 0.0 3 .. 0 120 FTG PE 0.0
181 28.8 0. tZI H3.9 ,~" tZI tZI. 010 TL 8.00 Pl..' 0. 1
Pipe: 49 --35. 1 2.203 PL 8.00 PF 0. 1
181 28.8 0.0 83.9 0.0 3.0 120 FTG PE ei. tZt
182 28.8 0.0 8"•· 0 0.0 0. ll.110 TL 8.00 PV 0. 1
Pipe: 50 -·-35. 1 2 .. 21213 PL 8.00 PF 0. 1
182 28.8 !t'.l. ll' 84 .. 0 0. It) 2;. 0 120 FTG PE 0.0
183 28.8 0. tZl 8.lt. 1 •Zt. 0 0.010 TL 8.00 PV 0. 1
Pipe: 51 -35. j_ 2.203 PL 8.00 PF 0. 1
183 28.8 0. 0 8.lt. 1 tZl. 0 3.0 120 FTG PE 0. 121
184 28.8 0.0 Bi►• 2 0 .. lt'.l 0.010 TL 8.00 PV 0. 1
Pipe: 52 ·-3~:5. 1 2. i.=::03 PL 30.67 PF 0. ~5
181+ 28.8 0. IZl 81+. 2 0. IL' 3.0 121l' FTG 2T PE 1. ;~
(:'. l 26.0 0.0 85.9 0. tZI 0.010 TL 50.67 PV tZI. 1
SPRIN~{LER SYSTEM HYDRr.:1ULIC AN(.'.\LYSlf> Page 9
JOB TITLE: HHB PH~4RMACEUT I Cf.'.:\LS
PIPE DATA (cont'd)
PIPE TAG Q(GPM) DIA<IN> LENGTH PRESS ..
END EL.EV .. NOZ. PT DISC. VEL(FPS) HW<C) <FT> SUM.
NODES <FT> < K > <PSI> <GPM) F. L. /FT <PSI>
Pipe: ~53 "-3Lt .. G 2.203 PL 2.83 PF t21. 1
22 26.0 0. 121 B3. i.::'. Q.'I. Q.'I 2.9 120 FTG T PE 1.2
22{~ 2B.8 0. 0 8~:'.. 1 0.0 0 .. 010 TL 12.83 ptJ 0. 1
Pipe: ~i4 -2;.1. •• 6 2. f:0~3 PL 139. 17 PF 1.4
i:.=~i='.t~ ~~B. 8 0.0 82. 1 0 .. 0 2. 9 120 FTG T PE ,~. 0
169 28.8 0.0 83.6 0.0 0.010 TL 11t9. 17 PV tZI. 1
Pipe: i:::-1::-...J...J ·-<~;Lt. G i::'.. i::'.03 PL 8. 00 PF 0. 1
1&9 28.8 0.0 83.6 0. Q) 2.9 j_ 21t.i FTG PE 0 .. 0
170 2H.8 0. 0 83.G 1Z1. tZl 0.010 TL 8.00 PV 0. 1
Pipe: 56 -34.6 2. 21Li3 PL 8.00 PF 0. 1
170 i::'.8. 8 0 .. 0 83 .. G ,21. 0 2.9 120 FTG PE 0.0
17l 28.8 0.0 83.7 0.0 fi. 010 TL 8.00 PV 0. 1
Pipe: 57 -34.6 2. i='.03 PL 8.00 PF 0. 1
171 28.8 It). 0 8:3. 7 Q.'l. ILi f:. s, 120 FTG PE 0. Q.'l
172 28.8 0.0 f.33. 8 0.0 121,. ILi 10 TL 8.00 PV 0. 1
pip€•: 58 -·3'+. 6 2.203 PL 8.00 PF 0. 1
172 28.8 0.0 83.8 0 .. 0 2.9 120 FTG PE 0.0
173 28.8 0.0 83.9 0.0 0.010 TL. 8.00 Pl.) 0. 1
Pipe: 59 --3Lt. G 2.203 PL B.00 PF tZI. 1
173 28.8 0.0 83.9 0.0 ;.:~. 9 120 FTG PE 0.0
1 7'+ 28.8 0.0 83.'1 0 .. 0 0.010 TL B.00 PV 0. 1 -~
Pipe: 60 -34.6 ;:::. f:03 PL 8.00 PF 0. 1
174 28 .. 8 0 .. 0 83 .. 9 0.0 2.9 120 FTG PE 0. 121
175 28.8 0.0 81+. !Li 0.0 0.010 TL 8. 00 PV l{.i. 1
Pipe: 61 "·"3.lt. 6 i.~ .. 203 PL 8.00 PF IZI. 1
175 f:8. a 0.0 BL1-. 0 ei. 121 2.9 12fli FTG PE 0.0
176 28.8 IZI. 0 84. 1 IZI. 0 0.010 TL 8 .. 00 PV 0 .. 1
Pipe: c-· "\C -34.6 ·~-203 PL 8.00 PF 0. 1
176 28.8 0.0 84. 1 0 .. 0 i~~-9 li::'.0 FTG PE 0. 0
177 28.8 0. 121 8Lt. 2 0n0 0.010 TL 8.00 PV 0. 1
Pipe: 63 ·-3it. 6 2 .. 203 PL 30.67 PF 0.5
177 28.8 0.0 8Lt. 2 0. 0 2.9 120 FTG 2T PE Li='.
23 2(;. 0 0.0 85.9 tZI.IZI 0.010 TL 50.67 PV 0. 1
Pipe: 64 --Lt2. ll.) 2.203 PL 2.83 PF 0 .-, • i::.
24 26.0 0 .. 0 H~3 .. 2 0,, 0 3.5 120 FTG T PE 1.2
24(4 28.8 0.0 8f::. 2 0.0 0. 01-l+ TL 12.83 PV 121. 1
Pipe: 65 -42.121 2.21213 PL 2121. 1210 PF 0. Lt
21+(:'.l 28.8 0. 121 82. i.:~ 0. 0 3.5 121li FTG T PE 1 ·=· . '--
•jC:-L-..J i='.G. 0 0.0 B3.8 0 .. 0 0.tZll.4 TL 30 .. 00 PV 121. 1
SPfH N~~LEF~ SYSTEM HYDHAULIC AN(4LYSIE~ Page 10
,JOB TITLE: ISIS PHARMACEUT I CAL~3
PIPE DAH~ (cont" d)
PIPE TAG n<GPM) DH4(1N) LENGTH PF<ESS.
END ELE\.1• NOZ. PT DISC. VEL..(FPB> HltJ ( C) <FT) SUM.
NODES (FT) 00 <PSI) <GPM) F. L. /FT <PSI>
Pipe: 66 ·--25. 3 ~~" i='.1213 PL 24.50 PF 121. 2
.-,c:-i:::. .. , 26. it) 0. l{.i 83.8 0.0 ·::, L... l 121li FTG 2T PE 0. 0
26 2G .0 0.0 8L~" 1 IZl .. ,::i 0 .. 0tZt~5 TL 44. ~S0 pl) 0. 121
Pipe: 67 --L•2. 0 ;~. 202; PL 87.00 PF 1. ·::· .._,
26 2G.0 0.0 84. 1 0.0 ---. r-..!, • ;::, 120 FTG T PE 0.0
~?.7 2€."\. 0 l{.i. 0 85. L► 0. 0 0. llH 1+ TL 97. 0tti PV 0. 1
Pipe: 68 -·-2i::'. .. 4 2.203 PL 7.tZltZI PF 0.0
27 2("\. 0 e,. 0 8~.:i. Lt 0. Ill 1. 9 121li FTG L PE Li='.
160 ~~B. 8 0. 0 8L►• 2 0 .. 0 0.004 TL 10.00 PV 0.0
Pipe: 69 --22. , ... 2. 21li3 PL 8. lt)0 PF l{.i. tti
160 28.8 0. 0 84.2 0.0 1.9 120 FTG PE 0.0
161 28.8 0.0 84.2 !Li. 0 0. 00L► TL 8.00 PV 0.0
Pipe: -NI -~::2 .. 4 1~: N 20:~ PL 8.00 PF 0. 10
161 i.:~8. 8 121. ti) BL►• 2 Ii.). 0 1. C) 120 FTG PE 0.0
16i::'. 2H.8 0.0 84.3 0 .. tZl 0.004 TL 8.00 Pl) ILi. 0
Pipe: 71 -22. L► 2.203 PL 8.00 PF !Li. 0
l.bi::'. i::'.8. a 0.0 84.3 121. 0 1.9 120 FTG PE 0.0
163 28.8 0. fl) 8.l•. 2:; 0.0 0. 012'.l'+ TL 8.00 PV 0.0
Pipe: 7;?.. -j~~i::'.. 4 i:::'.. 203 PL 8.00 PF ,21. 121
H,3 28.8 0. l{.i BL►• 3 0.0 1.9 121li FTG PE 0.0
164 28.8 0.0 BL1-. L1-,~. 0 0.004 TL 8.00 P\J tZl. 0
Pipe: 73 -22.4 2 .. 203 PL 8 .. 00 PF 0.0
164 28.8 0.0 84.4 0. 0 1.9 li:"::0 FTG PE 0.0
165 28.8 1t.'l. 0 84. LJ-0.0 0. 00'-► TL 8.00 PV 0.0
Pipe: 74 ---22. 4 2.203 PL 8.00 PF 0.0
165 28.8 0.0 84. Lt 0 .. 0 1.9 120 FTG PE 0.0
166 28.8 0.0 BL, .• L1-0.0 0. 00L► TL 8.00 PV 0.0
Pipe: 75 -"22 . .l► 2.203 PL 8.00 PF 0.0
166 28.B 0.0 8Lt. Lj. 0.0 1. I:) 120 FTG PE 0.0
167 28.8 0.0 84. ~5 ltJ. 0 0. 1t.'l01+ TL 8.00 PV 0.0
Pipe: 7C--. ·--22 ,. L► 2. ~~1213 PL 8.00 PF 0. IZI
167 28.8 0.0 81+. 5 0.0 1.9 120 FTG PE 0.0
168 28.8 0.0 84.5 0.0 0.004 TL 8.00 P\J 0.0
Pipe: 77 --22. 1► 2.203 PL 5.50 PF 0. 1
168 28.8 0.0 8l1-. 5 0. 1Z1 1.. I:) 120 FTG T PE 1 -::, • L...
28 26. !Li 0.0 85.8 0.0 1t.'l. 004 TL 15.50 pt.,• 0.0
Pipe: 78 -42.0 3.31 Lt PL 25. 17 PF 0. 1
28 26 . l{.i 0.0 85.8 0.0 1.6 121Li FTG 2T PE:. 0.0
2':t 26.0 0.0 (35.9 0.0 0.002 TL 55. 17 PV 0.0
SPRINKLER SYSTEM HYDHAULIC ~~NAL YSI S Page 11
·JOB TITLE: ISIS PHt~RMACEUT I Cf-1L.S
PIPE DATA (cont'd)
PIPE T(~lG Q(GPM) DIA<IN) LENGTH PRESS.
END ELEV. NOZ. PT DIBC .. VEL<FPS) Hl.-J ( C) <FT> SUM.
NODES <FT> < K) <PSI) (GPM) F.L./FT <PSI>
Pipe: 79 ·--l.6 .. 7 c~. 203 PL 56. 50 PF 0.2
25 26.0 0. e1 B3.8 Q). 0 1. , .. 12'21 FTG L►T PE 0. 0
26 i~6. 0 0.0 84. 1 0 .. 0 0. 0,:'.13 TL 96.50 PV 0.0
Pipe: 80 -t9.6 2.203 PL 11.00 PF 0. tZt
27 26.0 Ii). 0 85. L,-,~,. 0 1.6 120 FTG L PE 1.2
151 28.8 0.0 EV+. ~~ 0. 12t It). 003 TL 14.00 PV ll,. Ji.)
Pipe: 81 --l 9. 6 i~:'.. 2ti.)3 PL 8.00 PF 0. e,
151 28.B 0.0 £:v ... 2 IL•. tZl 1..6 120 FTG PE 0.0
152 2H.8 0.0 l:)L,-• 2 0.0 0. 003 TL 8.00 PV 0. e,
Pipe: 82 -19.6 i~. 203 PL 8.00 PF 0.0
15~:'. 28.8 0.0 8L1-. 2 0.0 1..6 120 FTG PE 0.0
153 28.8 0.0 84.3 0. lli 0.003 TL 8. 0ft) PV tZt.tZt
Pipe: 8""' ,.J --19 .. 6 2.203 PL 8.00 PF 0. 12'
152; 28.8 It). 0 BL•. 3 0.0 1. 6 1 ;~0 FTG PE !Li. 0
154 28.8 0.0 84.3 ~?I. 0 0.003 TL 8. 00 PV 0. fZI
Pipe: 84 -19.6 ;:::. f~03 PL 8. 01t.i PF 0.0
154 28.8 0.0 BL •• 3 0.0 1.6 120 FTG PE 0.0
155 28.8 0. 0 84.3 0. l{.i 0. 003 TL 8. 0Qi PV 0. 0
Pipe: B~3 ·--19. f, 2.203 PL 8.00 PF 0.0
1 ca:::· __,._, 28.8 0. 0 84.3 IL•. 1t.i 1.6 12'21 FTG PE 0.0
156 28.8 0.0 84.4 0.0 0.003 TL 8.00 PV 0. Q) . ..,
Pipe: 86 --19.6 2. i:~03 PL 8.00 PF '21. 0
156 28.8 0. 0 8L1-. 4 0. ~:'.I 1.(, li~0 FTG PE 0.0
1 t57 i::'.8. 8 0. e1 B4.4 0.0 e1. 003 TL 8.00 PV 0.0
Pipe: 87 --19. 6 2. 20~3 PL 8.00 PF 0.0
157 28.8 0.0 f:V~. L~ 0. IL• 1.6 121l) FTG PE 0. 0
158 28.8 0.0 B4.4 0.0 0. 0,:'.13 TL 8.00 PV 0.0
Pipe: 88 -19.6 2.203 PL 8. 1{)0 PF It.,. 0
158 i::'.8. 8 0.0 84.4 0.0 l.. f~, li~0 FTG PE 0.0
159 28.8 0. 0 84. 1► tZt. 0 0.003 TL 8.00 PV tZt .. tZI
Pipe: 89 ·--l. 9. 6 2. i::'.03 PL 17.50 PF 0. 1
159 28.8 0.0 84. L► l{.i. tZt 1.6 120 FTG 2T PE 1 .-. • a::..
28 26.0 0.0 85.8 0.0 0.003 TL 37.50 PV 0. 121
Pipe: 90 0.0 2.703 PL 18.00 PF 0.0
201 28.8 0.0 82.0 0.0 0.0 120 FTG PE 0.0
20i:~ 28.8 0.0 82. l{.i Ill. Qt 0.000 TL 18.00 PV tZl.0
Pipe: 91 0. 1 2.703 PL 15.00 PF 0.0
202 28.8 0. 0 BE::. e1 ll). 1t.i 0. 0 120 FTG T PE 0.0
30A i:~B. 8 0. 0 8i~. 121 0.0 0. 00121 TL 27.00 PV 0.0
SPRINKLER SYtHEM HYDRAULIC ANf=tLYSIS Pa~1e 1 .-, C
JOB TITLE: ISIS PHt~RMACEUT I Cf.\LS
PIPE Dr.:lTr.:1 (cont'd)
PIPE Tr-lG G! <GPM> Dln(IN) LENGTH PREE,S.
END ELEV. NOZ. PT DISC. ~JEL <FPS) Hl--J <C> <FT> SUM.
NODEB (FT) no <PBI) (GPJYJ) F. L... /FT <PSI)
Pipe: 92 tZI. IZt 2.703 PL 210.00 PF Qt. ,21
3t2tA 28.8 0.0 82.0 lt,l. IZI 0. ti.) 12121 FTG T PE 1 .-, "C
30 26. tZI Qt.Qt l3~3,. ~::: Qt• ~~I 0. 01,)0 TL 222.00 P\.' 0. e,
Pipe: 93 0.0 2. 202:; PL 3.00 PF 0.0
i::'.Ql3 28.8 0.0 Bi:::. 0 0. Ii.) 0.0 li='.0 FTG T PE ~!'.I. IZt
31Ztf.:l 28.8 0.0 82. Qt Ill. 0 0.000 TL 13.00 PV Ill. 0
Pipe: <:) l► 0.0 2. 21z13 PL 16.00 PF 0.0
f~IZt4 28.8 0.0 8i::'.. 2 0.0 0.0 12fli FTG PE 0.0
205 28.8 ~~-0 f32.2 0.0 0.000 TL 1(,. 00 PV 0.0
Pipe: 9 :_; 0.0 i::'.. 203 PL 16.00 PF 121. 0
205 2B.8 0.0 s·=· •:::, ,_. I.... 0. fi 0. ~~) li::'.0 FTG PE ,!'.I. 121
206 28.8 0.0 8i::'.. 2 0. Ill 0.000 TL 16.00 PV 0.0
Pipe: 96 --0. tZl ;~. i::'.03 PL 1.00 PF 0.121
206 28.8 0.0 A·-·, .-, \.,.;C.e C 0 .. 0 0.0 12121 FTG T PE 0.0
i::'.4t➔ i:~8 . 8 0.0 Bi:.~. i::'. 0. Ill 0.000 TL 11.00 PV ~~-12,
Pipe: 97 0.0 2.203 PL 16.00 PF 0.0
i:~07 2B.B 0.0 a·::'J L.... 1 0 .. 0 0.0 li::'.0 FTG PE 0.0
i=~lt.18 28.B Q.i. 0 82. 1 1Zt. f2t 0. 0012.i TL 16.00 pt) 0.0
Pipe: 98 0. ti.) 2.203 PL 16.00 PF 0.0
208 28.8 0.0 82. 1 0. tZt 0.0 120 FTG PE 0.0
~::09 28.8 0.0 a·=-L.... 1 ~~-0 0.000 TL 16.00 PV 0 .. 0
Pipe: 99 -0.0 2. 202:; PL 1. 00 PF 0.0
209 28.8 0.0 a·::'J a;;... 1 0.0 0. 0 120 FTG T PE 0.0
22(.'.l 28.8 0.0 82. 1 0.0 0.000 TL 11.00 PV 0. tZI
Pipe: 100 3i::'.. 9 4.310 PL 4.50 PF 0.121
1 2[,. 0 0 .. 0 83 . .lt, 0. 1t,i 0 .. 7 120 FTG PE 0.0
4 26.0 0.0 83.4 0.0 0.000 TL 4.50 P\J 0.0
Pipe: HH (,6 .. 9 4.310 PL 12.00 PF 0. 0
L• f~{;. 0 0.0 B3 .. 4 0. ILi 1. ~5 1~::0 FTG PE 0 .. 0
6 26.0 0.0 83 • .l► 0.0 lli. 001 TL 12.00 PV 0.0
Pipe: 102 H.il. ''..'I Lt,. 310 PL 1 i::'.. 00 PF 0.0
6 26.0 0.0 3-:;• .l ..,J,. .. 0. li..'l ·::, ·::, '-". '-" 120 FTG PE 0. t;:.i
8 26.0 0. 0 83.4 0.0 0. 0tZt3 TL 12.00 PV 0.0
Pipe: 103 l3~i. 4 L►• 310 PL 12.00 PF 0. 1
8 26.0 0. 0 8.3. i► 0.0 3.0 U::0 FTG PE 0.0
10 26.0 0. 0 82;. 3 0. 0 0.005 TL 12.00 PV 0. 1
Pipe: 104 1 70. :~ 4.310 PL 7.92 PF 121. 1
10 26.0 0.0 a -;• -..~ ..., . ..., 0.0 -, ---~. I 120 FTG PE 0.0
12 26.0 0.0 83.3 0.0 0.007 TL 7.92 PV 0. 1
SPRIN~{LER SYSTEM HYDF<AULIC ANALYSIS Page 12;
JOB TITLE: H3IS PHAHMACEUTICALS
PIPE Df.HA (cont:' d)
PIPE H4G G! <GPM) DI~~(IN> LENGTH PRESS.
END ELEV. NOZ. PT DISC. t,,'EL ( FP~3) Hl--J (C) <FT> SUM.
NODES (FT) ( K) (PSI) <GPM) F. L. /FT <PSI)
Pipe-?: 10~5 21Z1~5. -~ .. ., 4.310 PL 12.00 PF 121 .. 1 1 .-, .::. 26. fl' 0.0 83.3 fl,. 0 I ,~• ·'-1-. '.:) 120 FTG PE 0.0
14 26.0 0.0 B3. 1 ,::. . 0 0. 010 TL 12.00 PV 0. 1
Pipe: 106 2Ld. 0 J.i .• 3H.1 PL 7. 0lt) PF 0. 1
14 26.0 0.0 f33. 1 0 .. 0 5.3 120 FTG PE 0.0
1 '+A 26.0 0.0 83. 1 121 .. Ii.) e,. 12113 TL 7.00 PV 0.2
Pipe: 1 tZl7 -·-183. f~ 1 •• 3 lit) PL 5.00 PF 0.0
14A 26.0 0. 0 83. 1 0.0 L•• 0 12fl'l FTG PE 0.0
16 2E.,. 0 0.0 i:3~3 .. l 0 .. 0 0 .. 00B TL 5. 00 pt; 0. 1
Pipe: 108 --11•7. 2 4.310 PL 12.00 PF 0. 1
16 i::'.6. 0 0.0 83. 1 0.0 3. i~ 120 FTG PE 0.0
18 26.0 0. It) 8~;. 2 "-'· 0 0. @Zt5 TL 12.00 PV 0 .. 1
Pipe: 109 -·-11 l.. 8 4.310 PL 12.00 PF 0.0
18 f:6. 0 0.0 83.2 "-'· f' 2. ~) 120 FTG PE 0.0
20 26. 0 0.0 B3.2 ti). 0 0 .. 003 TL 12. 00 PV 0. 1Z1
Pipe: 110 -7( ..... 6 .L •• 31f' PL 9. 5'+ PF Q.1. 0
20 26.0 0.0 83.2 0. 0 1..7 120 FTG PE 0.0
2i.~ 26.0 0. 0 82:. i::: 0.0 0.002 TL 9. 5 1+ PV "-'· 0
Pipe: 111 ·--.l•2. 0 4. 3.10 PL 16.00 PF 0. Qt
2f~ 26.0 0. "-' 83. i.:'. 0 .. It) 0.9 12ft) FTG PE 0.0
i::'.4 i::'.6. 0 0.0 83. ;::: ,!:t. 0 0.001 TL 16.00 PV 0. IZt .1,,
Pipe: 112 0. Ill i, .• 310 ~=•L C).00 PF 0.0
24 26.0 0.0 B3. i2 0.0 tZI. 0 1 i::'.0 FTG PE 0. Ii.)
3tt) 26.0 0 .. 0 8~3. 2 fl1. e, 0. 001l' TL 9.00 PV 0.0
Pipe: 113 ·--32. <) 6.403 PL 12.00 PF 0.0
3 26.0 0.0 B6. t21 0 .. e, 0 .. 2; 120 FTG PE 0 .. 0
r::.-,.J i:::E,. 0 0.0 86.0 0 • 0 0.000 TL 12. tZIIZI PV tZI. 0
Pipe: 11 1► -66.9 6 .. 4tt13 PL 12.00 PF 0.0
,::.-26.0 0.0 B6.0 0.0 0. 7 120 FTG PE 0. 121 .. J
7 26. fl' 0.0 8( ..... 0 0.0 0.000 TL 12.00 PV 0.0
Pipe: 11 ~=-j "·-101. 1 (,. 403 PL 12.IZIIZI PF 0. Qt
7 26.0 ei. e, 8(.... tZI 0.0 1. fl) 12Q.' FTG PE 0. tZI
'·) ~::(;. 0 0. 0 H6.0 0.0 0.000 TL 12.00 PV 0.0
Pipe: 116 -135. I.. ( .... 403 PL 12. 00 PF tZI. 0
<) i.~6. 0 IZI. 0 f:36.0 0.0 1.3 120 FTG PE 0. e,
1 1 26.0 0.0 86.0 0 .. 121 0 .. 0flH TL 12.00 P~' 0 .. 0
Pipe: 117 -170.3 t., • lt-03 PL 5.29 PF 0. e,
1 1 26. t2l 0.0 86. 121 ft). 0 ·1. 7 120 FTG T PE "-'· 0 31 2E,. ILi 0. 121 86.0 0.0 0.001 TL 35.29 Pt..' 0.0
SP H I N ~(LE f< SYf:>TEM HYDH~~ULIC ANALYSIS Page 14
JOB TITLE: IBIS PHAliMACEUT I Cf.:'.\LB
PIPE D(Hf.:l (cont'd)
PIPE TAG G! <GPM) DI~~<IN> LENGTH PRESS.
END ELEI..). NOZ. PT DISC .. VEL(FPS> Hl.-J <C> <FT> SUM.
NODES (FT) 00 <PHI> <GPM> F. L. /FT <PSI)
Pipe: 118 -·-424. 1 6.403 PL 22.75 PF 121. 2
31 26.0 0.0 86. e, 0. It) LJ,,. 2 12ti..'t FTG L PE 0 .2
TOR i.'.::5. 5 0.tZI BG. 1+ c::i. 0 0.006 TL 31.75 p1.,1 0. l
Pipe: 119 -1.2, ... 1 6. L1-03 PL 25.00 PF 0. j_
TOR 2~5. 5 0.0 B6.4 0.0 .t'.1-. 2 120 FTG PE 10.B
BOH flt. 5 H. S. 97. LJ, ~50. Q.i 0.006 TL 25.00 PV 0. 1
Pipe: li::'.0 ···-4 7 £J,. l 8.510 PL 1121. 00 PF 0.121
BOF< 0. ~:i H. S. 97. LJ, 50 .. 0 i='.. 7 111-0 FTG L PE 1.5
U5 --3. 0 0 .. 0 9B.9 IZt. ILi 0.001 TL 21.97 PV 0.0
Pipe: 121 -••i· 7 '-•. 1 7.987 PL 260.00 PF 0. 5 ur:::-'-' --3. 0 0.0 9B.9 0. ~~ 3.0 150 FTG 7L PE ;=.:. 2
U4 ~~-0 0. ti..'t 97. -:,·♦ ..... 0. 0 0.002 TL 355.20 p1.,1 0. 1
Pipe: li::'.2 FIXED PREGSURE LOSS DEVICE
U3 i.~. e, 0.0 102. 3 0 .0 5.0 psi, LJ, 7LJ-. 1 gpm
U4 i:~. c::i 0.0 97.3 0 .. ti..'
Pipe: 122; --1· 7 .l.1-. 1 7.987 PL 12.00 PF 0. 1
U3 2.0 0.0 10i::'.. 3 0.0 3.0 150 FTG T2L PE i=.: •. 2
u·=· '----2;. 0 0.0 1 fl't.l.J,. 6 0. 0 0.002 TL 84.53 PV 0. j_
Pipe: li:~4 ·-474 . i::'. 7.987 PL LttZI. 00 PF 0. 1 u--, C. --3. 0 0 .. 0 10-4. 6 0.0 3.0 150 FTG TG PE 0.0
Ul --3 . IZI SRCE 10L~. 7 (NIA> 0 .. 00i::'. TL 89.87 PV 0. 1 -~
Pipe: 1 i::5 -1+2. 0 6. 1+03 PL 12.-00 PF 0 .0
29 26.0 0.0 85.9 ILi. QI 0 . Lt 120 FTG PE 0.0
23 26.0 0.0 85.9 0. !Li 0. 0Qi0 TL 1 2 .00 PV 0.0
Pipe: 126 --76 . 6 6.403 PL 9.54 PF 0. tZt
23 2fa.0 0. 0 8~j. 9 flt. 0 0.B i.20 FTG PE 0. tZt
21 26.0 0.0 85.9 It). 0 0.000 TL 9 .. 54 PV 0. IZI
Pipe: 127 -11 1. 8 6 • .l.•03 PL 12.00 PF 0.0
~~ 1 i::'.6. 0 0. tZI 85.9 0.0 1. 1 1 i::'.0 FTG PE 0.0
19 26. e, 0.0 85.9 0.0 0.000 TL 12.00 PV 12). 0
Pipe: li:~8 ·--1'+7. 2 6. 41213 PL 12.00 PF 0. tZt
19 26.0 fl). 0 85. ':) ll'i. 0 1.5 1 i='.0 FTG PE 0.0
17 26.0 0.0 B5.9 0.0 0u001 TL 12.00 PV 0.0
Pipe: 129 -183. E:: 6. L►fl.t3 PL 12.00 PF 0.0
17 26.0 0. 0 85.9 0.0 1.8 li:.=~0 FTG PE 0. 0
15 E::6. 0 0.0 85.9 0.0 0.001 TL 12.00 PV 0. 0
pip<~: 130 -·-21 B. 9 6 .403 PL 12.00 PF 0. Q)
15 i.~6. 0 0. 0 85.9 0. e, 2. f: 120 FTG PE 0 .0
13 26.0 0.0 135.<) 0 .0 121. 002 TL 12.00 PV 0.0
SPRINKLEH SYSTEM HYDRAULIC r.1NAL.YSI S Page 15
JOB TITLE: ISIS PH~➔ RMACEU TI C~1L S
PIPE DATA (cont'd)
PIPE T~:1G G! (C:iPM> DH'.l(IN> LENGTH PRESS.
END ELEV. NOZ. PT DISC. \.'EL (FPS> HW<C> (FT> SUM.
NODES <FT> 00 <PSI) <GPM> F. L .. /FT < PE, I)
Pipe: 131 ···-253. 9 (,. 403 PL i::'.. G2 PF Ii.)" 1
13 26. flt flt. tZl f.\5.9 e,. e, .-·, c::-c:. ... J 120 FTG T PE Q.t. 0
---1 .. _:!-26. Ill 0. tZI B6 .. 1Z1 1Zt. 1,1 0.002 TL 32. (:,2 PV 0. IZI
Pipe: l 2:;f: Q.'i. !Lt L 101+ PL 10.00 PF 0.0
301 11. 2 0.0 47 .. 9 0 .. 0 0. 0 li::'.0 FTG PE t,1. 121
:30;.~: 11. 2 0 .. flt ./.► 7. 9 tt.'i. 0 0. 00Q.'i TL 10.00 PV 0.0
Pipe: 133 0. ,zi 1. 1•5i:~ PL 1 e,. 00 PF Qt. IZI
3e,i::: 11. 2 0 .0 '+7. g 0. !Lt e,. 1t.1 120 FTG PE Q.i. 0
303 11. 2 0.0 Li-7. 9 0.0 ILi. 01t.10 TL 10.00 P\.' Qt. IZI
Pipe: 1 ~31+ 0. 0 1.687 PL 3.00 PF 0.0
303 11. 2 0.0 1• 7. 9 '=-'· tZI 0.0 120 FTG ET PE 0.3
50 10.6 0.0 .1.,.g_ 2 C:.'i. 0 0.000 TL 15.00 PV 0.0
Pipe: 135 IZI. 0 1.452 PL 10.00 PF 0.0
30-4 11. 2 fl'i. 0 .lt9. ~; Q.i. !Li 0. !Lt 120 FTG PE 0.0
305 11. 2 0.0 L►<). ~S ,z,. 0 ILi. 000 TL 10.00 PV 0.0
Pipe: 136 lt.'i. ,~ 1. L►5i:~ PL 10. 01{) PF 0.0
305 11. 2 0. e, '+9. 5 0.0 0. tZI li='.0 FTG PE 0.0
3t2.i6 11. 2 0.0 1.,.9. ~; !Li. 0 0. 01/)Q) TL 10.00 P\.' 0.0
Pipe: 137 ···-0. 0 L 687 PL 3.00 PF 0. Qt
306 11. 2 0.0 Lt9. 5 fl'i. Ql 0.0 12e1 FTG ET PE 0.3
51 10.6 0.0 1►9. 7 0.0 0.000 TL. 15.00 P\.' 1Z1. 0
Pipe: 138 ,zi. 0 L 1 QIL• PL 13.00 PF 0.0
307 11. ~s 0. 0 ~:.50. 9 0.0 0. ~~ 120 FTG E PE 0 .. 121
308 11. ~j 0.0 50.9 0.0 flt. 000 TL 15. fli0 PV 0.0
Pipe: 139 0. 0 1. 452 PL 10.00 PF tZI. ,zi
308 11. 5 0.0 5,zi. 9 It~. 0 ll'i. 0 120 FTG PE !Li. 0
30<) 11. 5 0. IZt 50.<) 0.0 0.000 TL 10.00 PV 0.0
Pipe: 1 1+0 0.0 1. (-.87 PL 10.00 PF 0.0
309 11. ~:j 0.0 50.9 e,. 0 0. t2t li::!0 FTG PE 0.0
310 11. 5 0. t2t 50.9 tt'.l. 0 0.000 TL 10.00 PV 0. Ill
Pipe: 1 "• 1 0.0 1.687 PL 3.00 PF 0.0
310 11. ~i 0.0 50.9 0. ,zi 0.0 1f:0 FTG ET PE 0.4
52 10.G 0.0 51. 3 0.0 0. 0012, TL 15.00 PV 0. tZ1
Pipe: 1 L►2 --0. 0 1. 101+ PL 3.25 PF 0.0
311 11.~:~ 0. 0 ~:Si~~. 4 0.0 0.0 li::'.0 FTG 2T PE 0.3
53 10. l-. e,. 0 ~i2. 8 0 .. 0 0.000 TL 17 ·::,c ..., • a;;;.._1 ~•\,' 0.0
Pipe: 143 0.0 1. 104 PL 3.25 PF 1,:1. 0
312 11. 3 0.0 53.8 1/..l. tZl 0.0 120 FTG 2T PE 0.3
~54 10.G 0.0 5L►,, 1 ,~. 0 0.000 TL 13.25 P\.' 0.0
SPRI N~\LEH SYSTEM HYDf<AULIC ANALYSIS Pc:tge 16
JOB TITLE: ISIS PHAHMACEUT I Cf~L S
PIPE D~nr.:1 (cecnt"cl)
PIPE T{-\G Gi <GPM) DH~< IN) LENGTH PRESS ..
END ELE V .. NOZ. PT DISC. l,,'EL (FPS ) Ht.,.J (C) (FT) SUM.
NODES <FT) 00 <P£H ) <GP M) F II L.. /FT <PSI)
Pipe: 1 l.t4 0.0 1. 4~52 PL 10.00 PF 0 .. ei
313 11. 2 0. I{) 55. ~s ,21. 0 0. Q) 12e1 FTG PE 0.0
31 '+ 1 Li:.~ 0 .. 0 ,:::-r.::-r.:.~ ,J,.J .... J 0.0 0. 12)00 TL 10. 00 PV 0. ,21
Pipe: 145 -,t-'. e, 1. €,B7 PL 3. l{.10 PF 0. l{.i
3 1 '-t 11. i::'. 0. tZI 1::-i:::-r.::-... J...J. ,.J 0. ~'.) 0. Q1 1;:::0 FTG ET PE Qi. 3
c::-i:::· ...J...J 10. E., 0. Qt 55.7 It). It) 0.00121 TL. 15. Q)0 PV l{.i. 0
Pipe: 1 '-t6 ···1+i::'.Lt. 1 3.314 PL 11. 50 PF 1. 6
5121 10.6 0.0 48. i::'. ,~i. 0 15.8 120 FTG PE 0.0
51 10. (; 0.0 .lt9. 7 0.0 0. 137 TL 11.50 P\.' 1. 7
Pipe: 1.l• 7 ... 1.21 •• 1 3.31 1• PL 11.75 PF 1. 6
~) 1 10. (; 0.0 1+9. 7 Ill. 0 15.8 U::0 FTG PE tZI. 0
52 112.i . E., 0.0 51. -;, ..... Q.1. 0 0 .. 137 TL 11. 75 pl.,' 1. 7
Pipe: 148 ···4i::'.Lt. 1 3. 31 Lt PL 10.50 PF 1 • .lt
52 1121. 6 l{.i. l{.i 51. 3 0.0 i~i. 8 120 FTG PE 0. l{.i
53 10.6 0.0 52.8 0.0 0. 137 TL 112'. 50 pl) 1. 7
Pipe: 1 l►C) --1.21. •• 1 3. 31 it, PL 10 .. 00 PF 1., Lt
r·-. ~.:, 10.6 0.0 52.8 0.0 1 ~5. B 120 FTG PE 0. IZt
54 10.6 0.0 5.1. •• 1 0.0 l{.i. 137 TL 10.00 PV 1..7
Pipe: 1 ~50 ····4i::'.Lt-. 1 3.314 PL 11.75 PF 1. (:,
54 10.6 Ii..~. 0 54. 1 0.0 15.8 1212.1 FTG PE 0.0
c:.-1:::-...J...J 10.6 0.0 55.7 Ii.). 0 0. 137 TL 11. 75 PV 1.7
Pipe: 1 :.ii --L►2L►• 1 3. 31 1• PL 80.83 PF 13. 1
55 10.6 0.0 55.7 Ii.). Qt 15.8 120 FTG T PE 0.0
56 11£1. 6 0.121 68 .. 8 l{.i. 121 0. 137 TL 95.83 PV 1. 7
Pipe: 152 ···42L►• 1 3.314 PL 65.67 PF 1 i~. 1..
56 10. ('\ 121.0 €."' B. 8 0.0 l ~5. 8 120 FTG T2L PE 0.0
57 10.6 0. 0 81. i::'. 0.0 0. 137 TL 90. ('\ 7 PV 1. 7
Pipe: 153 --42.l•. 1 3. 31 l.1, PL 32. 50 PF 8.5
c=-·-, ...JI 10.G 0.0 81.i::'. 0 .. ti) 1 ~3. B 120 FTG i:::T PE G .. 7
14A 26.0 0.0 a -;• ..._,. 1 1£i. t2l 0. j -;_.-7
•'-' I TL 62.50 pl.) 1.7
Pipe: 1 ~5,,. i::'.9. Ii.) 1. 10Lt-PL 4.00 PF 2. i=~
1R 11. c:· 0.0 i::'.8. 9 0. IZt C). 7 12,~ FTG ET PE 1. 1 ._J
lQ 9. 121 5.5 27.8 29.0 0.202 TL 11. 00 PV 0.6
Pipe: 1 c:-i:::· ...J...J 2'➔• t2t 1. 1121'+ PL 8. 00 PF 1. 6
2R 11. 5 0.0 3tZt. 5 0 .. 0 9.7 120 FTG PE 0.0
1R 11. 5 0. lli i::'.8. 9 Q.i. e, 0.202 TL 8.00 PV 0.6
Pipe: 156 29.7 1. 10Lt-PL 5.00 PF 2. ~:i
2R 11. ~i 0. 0 30. t.i 0. e, .g. 9 120 FTG ET PE 1. 1
2Q 9.0 t::' ,:::-...,,. ...J i::'.9. 1 29.7 0.210 TL 12.00 PV 0.7
SPRINKLER SYSTEM HYDF<AUL IC ~lNAL YSI S Page 17
JOB TITLE: ISIS PHARMACEUTICALS
PIPE DATr-1 (cont'd)
PIPE n:1G G! (CiPM) DIA<IN) LENGTH PRESS.
END ELE\.). NOZ. PT DISC. t.,,'EL <FPS) Hl.--J <C> <FT> SUM.
NODES <FT) 00 (PBI> <GPM> F. L. /FT <PSI)
Pipe: 1 ~57 ~5[3. 6 1. 1 tZIL► PL 1. •• 75 PF 8 .. 7
.1+!::i 10.6 l{.i. 0 39 .. 6 0 .. 0 19.7 121li FTG ET PE 0. 4
c~li 11. ~5 e,. 0 30. 1:::-,.J 0 .. ''.) 0. 7 L►2 TL 11.75 PV 2.6
Pipe: 158 58.6 :3. 31L► PL :35. 00 PF 0.2
t.H; H~. 6 0. tZl 39.8 l{J. tZl i~~-2 li::'.0 FTG 2L PE I~~. tZI
45 10 .. 6 0.0 2/-). 6 !Li .. 0 0. 001+ TL '•5. 00 pl) 0. tZ1
Pipe: 1 ~:j':'.) ·=•·7 1 1.. ltZl4 PL 1+. 00 PF 2.0 I.-I "
3R 11. 5 !Li. l{.i ..... c::· i::: ....... 1 ,~,. 0 9 .. 1 12Q.i FTG ET PE 1. 1
3Q 9.0 c:.-,:::-,J. ,J i::'.4. ~~ -::,·7
1-I • 1 ei .. 17B TL 11 • tZltZt Pt.,,' ei. 6
Pipe: 160 f~7. j_ 1. 101 ... f::tL 7.50 PF L -:;-,_,
L►R 11. ~s 0.0 i='.6. 4 e,. 0 9 .. 1 li:::'.0 FTG PE i,::t. e,
3R 11. 5 0.0 .-,r.::· ,::. ,J. 1 0.0 0. 178 TL 7. =.i0 PV Q.'1. 6
Pipe: 161 27.8 1. 104 PL 3. 2!5 PF 1. <)
i►R 11. 5 0. 0 26. '• 1t.i .. e, C, ~ . :3 120 FTG ET PE 1. 1
4Q 9.0 r.::-a:::-,J. ,J i:~5. 6 i::'.7 .. 8 121. 187 TL 10.25 PV 0.6
Pipe: 162 51. •• g 1. 101.. PL 9.75 PF 13.0
L►b 10. (; 0.0 39.B t,'.'.I. 0 18.4 120 FTG 2T PE 0. I+
i+f< 11. 5 Q.i. 0 26. '• Ii.). 0 0. 6~/7 TL 1 ':>. 75 PV 2 .. ~;
pip<~: 163 3i::'. .. ~) 1. 104 PL 5.00 PF 2.2
5R 11. 5 '-1). 0 3€,. 2 17.1 .. ,~ 10.'0 12Q.'1 FTG 2E PE 1.. 1
5Q 9 .0 5 .. 5 35.0 :~;;:.::. 5 121. 2~.:i0 TL 9. 00 PV 0. 8
Pipe: 1 (-,L► 32.5 1. 10-'• PL 3. 00 PF 2;,. 2
L,-E, 10.G 0.0 39 .8 0.0 10 .. 9 120 FTG 2T PE 0. I+
5R 11. 5 0.0 2~(~. 2 0. 0 0. 2=.iQ.1 TL 13.00 PV Q.i. 8
Pipe: 165 14G. 1 3.314 PL 10.00 PF 0. i:::'.
Lt-7 10.6 0.0 1.0. 0 0 .. 0 5. '+ 120 FTG PE 0.0
'-HS H) .. 6 tZl. 0 39.8 0.0 0.019 TL 10. 00 pt; 0. ;~
Pipe: 16E., 22. 5 1. 10L1, PL. 4 .. 75 PF 1.5
E,R 1 L ~S 0.0 1 7. 1 0 .. 0 7.5 120 FTG ET PE 1. 1
f~Q 9.0 5.5 16. 7 22. 5 12). 126 TL 11.75 Pt.,' Q.i. 4
Pipe: 167 2~~. ~.) 1. 104 PL 6.50 PF 0.8
7R 11. 5 0.0 18.0 0.0 ...., , ... I • .::, 1f'.0 FTG PE 0.0
6R 11. 5 0. ,21 1 7. 1 Qt. 0 0. 126 TL 6.50 PV 0 .. 4
Pipe: 168 22.8 1. 104 PL 7.25 PF 1.8
7R 11. ~) 0. 0 18.0 0.0 7.6 120 FTG ET PE 1. 1
7G! 9 .0 5. ~; 17.2 22. 8 0. 129 TL 14. 25 PV 0. L•
Pipe: 169 -'1-5. 3 1.. 10Lt-PL 7.50 PF 3.5
8R 11. 5 Q.'1. 0 21.4 0. 121 15. ·::• I..-120 FTG PE 0.0
7R 11. 5 0. 1,; 18.0 0.0 0. 4(.-,ft) TL 7 .. 50 pt; 1. 6
BPHIN~<LER SYSTEM HYDRf4ULIC ANALYSIS Pc::,g e 18
JOB TITLE: ISIS PHAl1MACEUT I Cf.'.~LF:,
PIPE D~HA (cont" d)
PIPE TAG G!<GPM) DH)(IN) LENGTH PF<ESS.
END ELEV. NOZ. PT DISC. t,,tEL (FPS) Hli-J (C) (FT) SUM.
NODES <FT> no <PSI) <GPM> F. L. /FT <PSI>
Pipe: 170 i:~5 . IL'! 1. H?l4 PL 4.75 PF LB
BR 11. 5 0. IL~ i::'.1. 4 ,:1 . 0 8. L1. 120 FTG ET PE 1. 1
8Q 9. ,~ c::-•=-... J .... J i::~IZI .. 7 i:..:~~5 .. ''.) 0" 1 ~)3 TL 1 L 75 PV 0.5
Pipe: 171 70. •:;, ..... 1. 101• PL 7.50 PF 18.2
47 10.6 0.0 LHZI .. 0 0.0 i::'.3 .. 6 li::'.0 FTG 2T PE 0.4
E\H 11. ~) 0.0 21.4 e,. 0 1. 039 TL 17.50 PV 3.7
Pipe: l 7i::'. 216 .. 4 3. :314 PL 10.00 PF 0.4
.C:•8 10.6 0.0 40. 1+ ,21. 0 8.0 1212.1 FTG PE 0. 0
47 10.6 li..'l,. 0 L•0 .. 0 0 .. 0 0 .. 039 TL 10 .. 00 PV 0. I+
Pipe: 17:3 ;~C:. 5 1. 11211+ PL -4 . 50 PF 1. 1
9H 1 L ~3 0. ,zi 16 .. 8 tZI" ti..'l 7 .. 6 li::'.0 FTG 2E PE 1. 1
9G! 9. e, 5.5 16.B 22. ~:_:; 0. 127 TL 8.50 PV e,. 4
Pipe: 1 7'-► ~~~:'.. ~5 1.. 1,z,4 PL 10.75 PF 1. 1..
10R 11. 5 0.0 18. 1 tt'.1. 0 7. 6 120 FTG PE 0. 0
9R 1:1.. 5 0.0 16.H 0.0 IL'!. 127 TL 10 .. 75 P\.' 0. '+
Pipe: 175 f::3. 0 1. 1121'+ PL 6.00 PF 1. _.,
l
101~ 11. 5 0.0 l 8. 1 0. I,~ 7.7 U::0 FTG ET PE 1. 1
l 0(~ 9.0 i:::· c:· ...J •.... , 17.5 23. lt'.I 0. 132 TL 13.00 P\...' 0. i.
Pipe: 176 45.6 1. 10.l• PL 7.50 PF -, i::.-
~-...J
11 f{ 11. 5 0.0 21.(-. 0.0 1 i:::· J,. 2; 120 FTG PE 0. 0
10H 11. !:S 0.0 18. 1 tZt.0 0 .. 465 TL 7.50 pt) L6
Pipe: 177 25. 1 1. 10L• PL 5.00 PF 1.9
llR 11. 5 0.0 ;::: 1. 6 tZl.tZI 8.4 120 FTG ET PE 1. 1
11Q 9.0 c.-,:-.:· ...J • ...J 2e1. g 25. 1 0. 1 cc::· ......... , TL 12. 00 PV 0. 5
Pipe: 178 70. 7 1. 104 PL 7.50 PF U3. 3
48 10.6 0. e, 1+0. 4 0. tZt 23.7 120 FTG 2T PE 0. 4
11 I~ 11. 5 0. 0 (:'.1. 6 0.0 1. 048 TL 17.50 Pl..' 3.8
Pipe: 179 32. (~ 1. 10.1.. PL 5.25 PF 2.3
12R 11.. 5 0. tZt 36. ~5 tZI .. tZI 10.9 li='.0 FTG 2E PE 1. 1
12G! 9.0 r::-c::· ,._, ..... , 2~5. 2 2:2. (, 1t.'.f:5l TL 9.25 PV 0 .. 8
Pipe: 180 32.6 1... 104 PL 4.00 PF 3.5
48 1121.( ... 0. 0 1.0 .. .1.. 0.0 10.c.:1 121l1 FTG 2T PE 0.4
12R 11. 5 tZt. 0 36.5 0. tZI 0. 2~31 TL 14. 00 PV tZI. 8
Pipe: 181 319.7 3. :H 1• PL 10. Q.10 PF 0.8
'-•9 10 .. 6 0.0 41.2 121. 0 11. '-) 12121 FTG PE 0. Qt
'+B 1 Q.1. (... 12.1. e, Lt-0. L• 0 .. 0 0.081 TL 10.00 PV 1.0
Pipe: 182 22.7 1. 101+ PL 4.50 PF 1. 1
13R 11. ::i 0.0 17. 1 0.0 7. E, 1i::'.0 FTG 2E PE 1. 1
13Q 9.0 i::.-1:::-... J • ...J l. 7. 1 2i:~. 7 0. 12B TL 8.50 pi..,1 0.4
SPRIN•{LEF-< SYSTEM HYDR~lULIC ANf.'.tLYSIB
JOB TITLE: ISIS PHAHMACEUT I Cf-1LS
PIPE Df.H(.4 (cont'd)
PIPE H-)G Q(GPM> DH~< IN) LENGTH
END ELE\.}. NOZ. PT DISC. \)EL (FPS) HW(C) (FT>
NODES <FT> ( •·~) <PSI> <GPM> F. L. /FT
Pipe: ll:13 2~:'.. 7 1. 10-4-PL 10. 7~5
11+R 11. 5 0. e, 1 B. ~5 i;:1 .. e, .. ..,
l • ("\ 120 FTG
13F! 11. !5 0.0 17 .. 1 0.0 0. 128 TL 10.75
Pipe: 181+ 23. -..·. ..... L 1121 1► PL L►,. 50
l.Ll-R 11. ~5 0.0 18.5 0 .. 0 7,,8 1;::::10 FTG ET
14G! 9. 0 i:::· c:-18. ll.i 2:~;. -. 0. 13~5 TL 11. 50 ......... '-' .:.,
Pi pr-2: 1B5 LJ-6. 0 1. 11214 PL 7. ~50
15R 11. ~i 0.0 i::'.i::'.. 0 !Li" e1 1 ~.:=.;. J+ 121l.1 FTG
14H 11. 5 0. Ill 18 .. 1:::-0.0 0. 4 7~:i TL 7.50 ... J
pip€•: 1£.\6 25.5 1. 10'+ PL 3. 1{)0
15R 11. 5 0. 0 i:::'.2. 0 e,. 0 8. ~:i 120 FTG ET
l ';.:jG! 9. 0 i:::-c::-.__I• ._I 21.5 .-•,i:::-c:...._, • ,::-._I 0 • 1 ~;9 TL 10.00
Pipe: 187 71.G 1. 104 PL 7.50
i+9 10.6 0.0 1►1. 2 fli,. 0 2.1. ... I[) 120 FTG 2T
15H 11.. ~5 0. e, ;:::2. 0 10. 0 1.073 TL 17.50
Pipe: 188 ~;2. 9 1. 104 PL 6.25
lGR 11.. 5 0.0 3·7 _ 2 0.0 11. 0 120 FTG i::'.E
lb(] 9.0 5.5 ~;:.~. -i, ~;i:~. g 0. i:~51+ TL 10.25
Pipe: 189 32. •=) 1. 11214 PL Lt,. 00
1.,.9 10.6 0.0 1+1. 2 121. fll 11. e, 120 FTG 2T
16H 11. 5 0.0 ;.3·7. 2 0. ,~ 0. 2~54 TL 14.00
Pipe: 190 L►21+ • 1 2;. 31 1► PL 51. 0,21
~j0 10. (; 0.0 48.2 0. ''.'.I 15.8 120 FTG
l+C) 10.6 0. Qi '+1. i=: e,. tZI 121. 137 TL ~ii. 00
NOTES:
( 1 ) Calculations vJere pe·rformed by the HASS 5. ~-~-0 com put er·
under· license no. 8'=)2f;\J521 granted by
HHS S 1•s.t£~ms, Inc ..
i::'.193 lianchwood Dr. ' N .. E ..
t=lt lanta, Gr.1 302A~:i
(2) The system has been balanced to provide an average
imbalance at each node of 0.001 gpm and a maximum
imbalance at any node of 0.09~ gpm.
Page 19
PRESS.
SUM.
(PSI>
PF 1.4
PE fli. 0
PV 0. '+
PF 1.6
PE 1. 1
PV 12t • .I.►
PF 3.6
PE 0. 0
p1..,1 1.6
f:)F 1. 6
PE 1. 1
P'..' 0.5
PF 18.B
PE 0. L►
PV 3. <j
PF 2.6
PE 1. 1
PV 0.8
PF 3.6
PE 0. 4
PV 0.8
PF 7. 0
PE 0. 121
PV 1.7
program
(3) Velocity pressures are printed for information only, and are
not used in balancing the system. Maximum water velocity in
any pipe is 24.0 ft/sec.
SPRINKLER SYSTEM HYDRAULIC ANALYSIS
JOB TITLE: ISIS PHARMACEUTICALS
(4) PIPE FITTINGS TABLE
Pipe Table Name: STANDARD.PIP
Pf-=lGE: F Mf.HER H ~lL.: DYt~rlFL Ht,.JC: L:~IL'l
Diiamet er Equivalent Fittin!] Len~lths in FE•e-t
(in) E T L C B G
Ell Tee L.NGELL CHl-~VL'J BFYtJLV GATVL \,,I
2 .. f~Ql3 ~.:i .. 00 10. lt)IZt 3. 0ft) 11 .. 00 6.00 1..00
2.703 6" 00 1 i:~ .. 00 4. ,210 11+ .. 00 7 .. e,~~ 1.. 00
3. 31'+ 7.00 15. 0e, 5. 0,~1 16 .. Q)IZI 10n00 1.00
L~. 31 IZI 10.00 i:~0. 00 6,. ~'.JIZt 22.00 12.00 4.00
6. -403 14 .. lt.i0 30. e11z1 9. tt)0 32.00 10. 0Q.'I 3. !l.'10
PAGE: (3 MATEFHAL: BLT HWC: L::0
Diamet:£~r Equi Vc:\l ent: Fittin~J Lengths in Feet
(in) E T L C B G
Ell Tee LNGELL CHKl)LV BFYVLV (:)AT t...1L V
1.. H:'.14 2.00 5.00 2. ''.J''.J ~'3 .. 00 6 .. 00 1..00
:l. 1..5~~ 3 .. 00 6. IL'l0 i:~. 0ft) 7.00 6.00 1..00
1.. 687 '-•· 00 8 .. 00 i::'.. 00 9.00 6. 121121 1..00
Page 20
A D
ALMCHF, DPtJLV
10.00 10.00
10.00 10. 0121
13 .. t;:.i0 10. 0Q.i
20.00 10 .. 121121
28.00 19 .. 00
A D
ALMCI-H~ DPt...'L\,,•
10. 1210 10. 12)0
10 .. 00 10. 1t.i0
10.00 10. tZtlZI
Page 21
JOB TITLE: ISIS PHARMACEUTICALS
WATER SUPPLY CURVE
p
R
E -
i-· . .... , ,-.
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u
r~ r ..
p
s
I
1 i::'.,~+
I
l 1 lZt+
*\\\\0\\\\\\\\\\\\\\
I >: \ \, , \, \ \ \ \, \ \, \, '\ \ \ \ \' \ \, \ \
I ~: <-·· l Q13. ~:.:; psi 1:¥.1 152;0 g pm
10ti)+ Fl ov-, Test Point
I
()QI+
I
81Z1+
I
I
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!==================~===========
20+ LEGEND
X -Required Water Supply
104.73 psi@ 524.2 gpm
10+
I 0 = Available Water Supply
107.38 psi@ 524.2 gpm
II
II
II
II
0 -i-·+-·-+· -----·-·-1---·------t--·--···-··-..... ·-1-·---·--·--·-..... ·---~-···-···-···---·-· -·--·---+· ·-·· ..... --.... -···-..... -·-·+---···-·-···--·-------·-·+----------·--·-·---· . t-
400 600 800 1000 1200 1400 1600 1800 2000
FLDW (GPM)
October 31 , 1996
1. PRODUCT NAME
VIKING HORIZON®MIRAGE®
Model 8-2 Concealed Pendent Sprinkler
UL and C-UL Standard Response
Sprinkler Base Part No. 09782
Cover Plate Assembly Part No. 09804
UL and C-UL Quick Response .and
. Factory Mutual Standard Response
• Sprinkler Base Part No. 09783
Cover Plate Assembly Part No. 09804
(See Footnote No. 7, Below)
Manufactured 1996-
2. MANUFACTURER
THE VIKING CORPORATION
21 O N. Industrial Park Road
Hastings, Michigan 49058 U.S.A.
Telephone: 1616! 945-9501 800 968-9501
Fax Number: 616 945-9599
From outside U.S.A.:
Jelephone: +1 (616) 945-9501
Fax Number: +1 (616) 945-9599
3. PRODUCT DESCRIPTION
The Viking Horizon® Mirage® Con-
cealed Sprinkler is a small, solder link
and lever spray sprinkler designed for
installation on concealed pipe systems
where the appearance of a smooth ceil-
ing is desired. The sprinkler is hidden
from view by a low profile, small diame-
ter cover plate installed flush to the ceil-
ing. The cover plate is available in sev-
eral decorative finishes to meet design
requirements.
The two piece design allows installation
and testing of the sprinkler prior to instal-
lation of the cover plate. After the sys-
tem has been tested and the ceiling fin-
ish applied, the "push on", "thriad off"
design of the Horizon® Mirage cover
plate assembly allows easy installation
of the cover plate with up to 1/2"
(12,7mm) adjustment available. The
"thread off" feature, is designed to pre-
vent unwanted disengagement of the
cover assembly, while allowing it to be
removed and reinstalled to permit tem-
porary removal of ceiling panels without
taking the sprinkler system out of service
and removing the sprinkler.
Inside the body of the Viking Horizon®
Mirage® Concealed Sprinkler, the de-
flector and sealing assembly are held in
position by the heat sensitive fusible link.
During fire conditions, when the tem-
perature around the sprinkler ap-
proaches it's operating temperature, the
cover plate detaches. Continued heat-
ing of the sprinkler causes the heat sen-
sitive fusible link to disengage; releasing
TECHNICAL DATA HORIZON® MIRAGE®
CONCEALED SPRINKLER
the deflector and sealing assembly.
Water flowing through the sprinkler ori-
fice strikes the deflector forming a uni-
form spray pattern to extinguish or
control the fire.
4. TECHNICAL DATA
Refer to chart (below, this page) for
approvals .
Rated to 175 PSI (1 207 kPa) water
working pressure
Factory tested pneumatically to 95 PSI
(655 kPa)
•· -
Spnng: U.S.A. Patent No. 4,570,720.
Thread Size: 1/2" (15mm) NPT
Orifice Size: Nominal 1/2" (15mm)
K Factor: 5.5 (7 ,9 Metric: for use when
pressure is measured in kPa)
Minimum operating pressure: 7 PSI
(48,3 kPa)
Viking Horizon® Mirage®Concealed
Sprinkler Installed in Acoustical Ceiling
Available Cover Plate Adjustment:
1/2" (12,7mm) +/-1/4" (6,4 mm)
Sprinkler Materials:
Body: Brass Casting UNS-C84400
Body Cap: Brass UNS-C26000
Deflector: Copper UNS-C19500
Deflector Pins: Stainless Steel
UNS-30300
Lever Bar: Copper Alloy UNS-C72500
Compression Screw:
Brass UNS-C36000
J 1~ ~1 l-==--==-I l J L ) (.
Fusible Link Assembly: Nickel Alloy and
Eutectic Solder
Fusible Link Levers: Stainless Steel
UNS-S31600
Seal: Teflon® Tape
UUC-UL listed
Standard Response
Part No. 09782
UUC-UL listed
Quick Response
FM approved Standard
Response
Part No. 09783
Sprinkler Nominal Highest Ambient Relulred
Temperature Temperature Temperature Allowed Cover ssembly
Classification Rating 1 at CelllnQ 2 Temperature Rating
Ordinarv 165°F (74°C) 100°F (38°C) 165°F(74°C)
Intermediate 220°F (104°C 150°F (65°C) 165°F 74°C)
Base Part No.3 Approvals4
UL6 C-UL 5•6 FM7 NYC8
09782 A1, 81 A1, 81 -A1, 81
09783 A2,82 A2, 82 A1 A2,82
Approved Temperatures Approval Listings
A-165°F (74°C) 1 -Listed Standard Response Sprinkler
B -220°F (104°C) 2 -Listed Quick Response Sprinkler
Footnotes
1. Temperature rating of Viking Horizon® Miragelfb Concealed Sprinkler is stamped on
the sprinkler body.
2. Based on NFPA-13. Other limits may apply depending on fire loading, sprinkler
location and other Authority Having Jurisdiction requirements. Refer to specific
installation standards.
3. Base part number shown. For complete part number, see price list.
4. This chart shows the listings and approvals available at the time of printing. Other
approvals are in process. Check with manufacturer for any additional approvals.
5. Listed by Underwriters Laboratories Inc. for use in Canada.
6. UL and C-UL listing is limited to smooth, flat horizontal ceilings.
7. Sprinkler Base Part No. 09783 is Factory Mutual Approved as a Standard Response
Sprinkler. (Note: Cover Plate Assembly Part No. 09804 MUST be used).
8. Accepted for use by New York City Department of Buildings. MEA No. 89-92-E Vol. X.
Note: Units of measure in parentheses may be approximations.
Form No. 021993
Replaces Sprinkler page 20 a-c dated July 8, 1996
(Added NYC Acceptance)
;>
Sprinkler 20 b
Spring: Nickel Alloy
Cover Plate Assembly Materials:
Cover Plate Assembly: Brass
UNS-C26000
Spring: Nickel Alloy
Solder: Eutectic
Cover Finishes:
Polished Chrome
Painted1 White (No. 1004)2
Painted1 Ivory (No. 1634)2
Painted1 Black (No. 1007)2
1 Painted finish consists of Polyester Baked
Enamel.
2 Sherwin-Williams• Color Answers™ Interior
Color Number. Other Colors available on re-
quest. See Sherwin-Williams* Color Answers™
Interior Color Selection color numbers.
Ordering Instructions:
To order the Viking Horizon® Mirage®
Concealed Sprinkler and Cover Plate
Assembly, refer to:
Sprinkler Base Part No. 09782 or09783
and Cover Plate Assembly Part No.
,.. 09804.
Specify sprinkler temperature rating
and temperature rating and finish of
Cover Plate Assembly.
(See Footnote No. 7, Page 20 a).
Accessories:
Concealed Sprinkler Wrench *
Viking PN 08336W/B
* Concealed Sprinkler Wrench PN 08336W/B is
required. Previous Viking Horizon Flush Sprin-
kler Wrenches appear similar, but are manufac-
tured with an outside diameter too large for use
with Horizon* Mirage*Concealed Sprinklers. A 1/2" ratchet is required (not available from Vi-
king).
5. AVAILABILITY AND SERVICE
Viking sprinklers are available through a
network of Domestic, Canadian, and In-
ternational Distributors. See the Yellow
Pages of the telephone directory for your
closest distributor (listed under "Sprin-
klers Automatic Fire") or contact The
Viking Corporation.
6. GUARANTEES
For details of warranty, refer to Viking's
current price schedule or contact Viking
directly.
7. INSTALLATION
WARNING: Viking sprinklers are manu-
factured and tested to meet the rigid
requirements of the approving agency.
The sprinklers are designed to be in-
stalled in accordance with recognized
installation standards. Deviation from
the standards or any alteration to the
sprinkler or cover plate assembly after it
leaves the factory including, but not lim-
ited to, painting, plating, coating or modi-
fication, may render the sprinkler inop-
erative and will automatically nullify the
TECHNICAL DATA
approval and any guarantee made by
The Viking Corporation.
A. Sprinklers are to be installed in ac-
cordance with the latest published
standards of the National Fire Protec-
ti on Association, Factory Mutual,
Loss Prevention Council, Assemblee
Pleniere, Verband der Sachver-
sicherer or other similar organiza-
tions, and also with the provisions of
governmental codes, ordinances and
standards whenever applicable.
Concealed sprinklers are decorative
sprinklers and may be considered
special purpose. Refer to the Author-
ity Having Jurisdiction prior to instal-
lation.
NQIE: Model 8-2 Cover Plate As-
sembly 09804 MUST be used for all
Factory Mutual Approved installa-
tions. Previous Model 8-1 Cover
Plate Assembly 0831 O may still be
used for UUC-UL installations.
B. Sprinklers must be handled with care.
They must be stored in a cool, dry
place in their original shipping con-
tainer. Never install sprinklers that
have been dropped, damaged in any
way, or have been exposed to tem-
peratures in excess of maximum am-
bient temperature allowed. Such
sprinklers should be destroyed im-
mediately.
C. Viking Horizon® Mirage® Concealed
sprinklers are not intended for use in
corrosive environments. Use only
sprinklers listed for corrosive environ-
ments when subject to corrosive at-
mospheres.
D. Use care when locating sprinklers
near fixtures that can generate heat.
Do not install sprinklers where they
will be exposed to temperatures that
exceed the maximum recommended
ambient temperature for the tem-
perature rating used.
E. Adequate heat must be ;rovided
when the Viking Horizon Mirage®
Concealed sprinklers are installed on
wet pipe systems. When installing
Viking Horizon® Mirage® Concealed
sprinklers on dry systems, refer to ap-
propriate installation guides.
F. The sprinklers must be installed after
the piping is in place to prevent me-
chanical damage. Before installing,
make sure the appropriate model,
style, orifice size and temperature
rating with the desired response
characteristic is used. Install the
sprinklers according to the following
steps:
1. Install all piping and cut the sprin-
kler drop nipple to position the
1 /2 11 (15mm) NPT outlet of the re-
ducing coupling at the desired
October 31, 1996
HORIZON® MIRAGE ®
CONCEALED SPRINKLER
Concealed
Sprinkler
Protective Shell
Concealed
Sprinkler
wrench**
Part No.
08336W/B
** A 1 /2" ratchet
is required.
(Not available
through Viking).
[J []
Figure A
elevation. The drop nipple must
be perpendicular to the ceiling
and centered in a 211 (50mm) di-
ameter opening in the ceiling.
2: With the sprinkler in the plastic
protective shell, apply a small
amount of pipe joint compound or
tape to the external threads of the
sprinkler only.
3. Use only the special wrench* de-
signed for installing Viking Hori-
zon® Mirage® Concealed Sprin-
klers. With the sprinkler in the
plastic protective shell, place the
unit into the wrench.
* Concealed Sprinkler Wrench PN 08336W/B
is required. Previous Viking Horizon Flush
Sprinkler Wrenches appear similar, but are
manufactured with an outside diameter too
large for use with Horizon* Mirage® Con-
cealed Sprinklers. A 1/2" ratchet is required
(not available from Viking).
4. Turn the unit clockwise to thread
the sprinkler into the 1 /2" (15mm)
NPT outlet of the coupling. DO
NOT use the fusible link to start or
thread the sprinkler into a fitting.
G. After installation, the entire system
must be tested in accordance with
the recognized installation stand-
ards. The test is applied after the
sprinkler installation to insure no
damage has occurred to the sprinkler
during shipping and installation, and
Form No. 021993
October 31, 1996
TECHNICAL DATA
I (--~==~ I ! __ ,, I ~g§§~~--
~-=-~-i.:---~
2" (50mm) \ i ,'
-.-----.-' ' I diameter 1 ' L
hole required. T C J
2-3/411
(69,8mm)
Maximum
Sprinkler 20 c
HORIZON® MIRAGE®
CONCEALED SPRINKLER
1/2"
(15mm}7
NPT '
' 2-1/411
(57,2mm)
l
2-3/411 Sprinkler 09782 shown.
Dimensions for Sprinkler
09783 are identical.
to make sure the unit has been prop-
erly tightened. If a thread leak should
occur, normally the unit must be re-
moved, new pipe joint compound or
tape applied, and reinstalled. This is
due to the fact that when the joint seal
leaks, the sealing compound or tape
is washed out of the joint.
H. After testing, repairing all leaks, and
installation and painting of the ceiling,
the cover plate assembly may be at-
tached.
1 . Remove the cover from the protec-
tive box taking care not to damage
the cover plate assembly.
2. Remove and discard the plastic
protective shell from the sprinkler.
(It is recommended to retain a
protective shell in the spare sprin-
kler cabinet. The internal diame-
ter of the special Horizon® Mi-
ra9e® Concealed Sprinkler Instal-
lation Wrench is designed for use
with the sprinkler contained in the
shell.)
3. From below the ceiling, gently
place the base of the cover plate
assembly over the threaded body
of the sprinkler protruding through
the 2" (50mm) diameter hole in
the ceiling.
4. Push the cover plate assembly
onto the sprinkler until the unfin-
ished brass flange of the cover
plate base touches the ceiling.
The maximum adjustment available,
is 1/211 (12,7mm). DO NOT MODIFY
THE UNIT. If necessary re-cut the
sprinkler drop nipple.
I. DISASSEMBLY: The "thread off" de-
sign of the cover plate assembly al-
lows the cover plate assembly to be
removed and reinstalled to permit
temporary removal of ceiling panels
without taking the sprinkler system
out of service and removing the sprin-
Form No. 021993
(69,8mm)
Figure B
kier. To remove the cover plate as-
sembly:
1. From below the ceiling, grasp the
cover plate and gently tum it
counterclockwise.
If it is necessary to remove the entire
sprinkler, the system must be removed
from service. See Maintenance instruc-
tions and follow all warnings and instruc-
tions.
J. RE-ASSEMBLY: The "push on" fea-
ture of the cover plate assembly al-
lows easy installation of the cover
plate.
1. From below the ceiling, gently
place the base of the cover plate
assembly over the threaded body
of the sprinkler.
2. Push the cover plate assembly on
to the sprinkler until the unfinished
brass flange of the cover plate
base touches the ceiling.
8. MAINTENANCE
NOTICE: The owner is responsible for
maintaining the fire protection system
and devices in proper operating condi-
tion. For minimum maintenance and in-
spection requirements, refer to the ap-
propriate National Fire Protection Asso-
ciation Pamphlet that describes care
and maintenance of sprinkler systems.
In addition, the Authority Having Juris-
diction may have additional mainte-
nance requirements which must be fol-
lowed.
A. The sprinklers must be inspected on
a regular basis for corrosion, me-
chanical damage, obstructions,
paint, etc. The frequency of the in-
spections may vary due to corrosive
atmospheres, water supplies and ac-
tivity around the device.
8. Sprinklers or cover plate assemblies
that have been field painted or me-
chanically damaged mustJ>e re-
placed immediately. Sprinklers
showing signs of corrosion shall be
tested and/or replaced immediately
as required. Installation standards
require sprinklers to be tested and, if
necessary, replaced after a specified
term of service. For Viking Horizon®
Mirage® Concealed Sprinklers, refer
to the installation standards and the
Authority Having Jurisdiction for the
specified period of time after which
testing and/or replacement is re-
quired. Sprinklers and cover plate as-
semblies that have operated cannot
be reassembled or re-used, but must
be replaced. When replacement is
necessary, use only new sprinklers
and cover plate assemblies.
C. The sprinkler discharge pattern is
critical for proper fire protection.
Nothing should be hung from, at-
tached to, or otherwise obstruct the
discharge pattern. All obstructions
must be immediately removed or, if
necessary, additional sprinklers in-
stalled.
D. When replacing existing sprinklers,
the system must be removed from
service. Refer to the appropriate sys-
tem description and/or valve instruc-
tions. Prior to removing the system
from service, notify all Authorities
Having Jurisdiction. Consideration
should be given to employment of a
fire patrol in the affected area.
1. Remove the system from service,
draining all water and relieving all
pressure on the piping.
2. Remove the cover plate assembly.
a. From below the ceiling, grasp the cover plate and gently tum
it counterclockwise.
3. Place a plastic protective shell
(from the spare sprinkler cabinet)
over the sprinkler to be removed.
Sprinkler 20 d
The internal diameter of the spe-
cial Horizon® Mirage® Concealed
sprinkler installation wrench is de-
signed for use with the sprinkler
contained in the shell.
4. Remove the sprinkler from the pip-
ing in which it is installed.
a. Using the special sprinkler
wrench, tum the unit counter-
clockwise to remove the old
sprinkler.
5. Install the new unit. Care must be
taken to replace the sprinkler with
the proper model, style, orifice
size, temperature rating and re-
sponse characteristics. A fully
stocked spare sprinkler cabinet
should be provided for this pur-
TECHNICAL DATA
pose.
Use of the correct Horizon® Mi-
rage® Concealed Sprinkler can
be verified by checking the fusible
link for the following identification
scheme:
UUC-UL Standard Response:
..... No Stripe
UUC-UL Quick Response illl.d
FM Standard Response:
. .... Purple Stripe
(Refer to Technical Data Page 57
a-c for additional information).
UUC-UL QREC:
..... Yellow Stripe
(Refer to Technical Data Page 58
a-c for additional information).
Replaces Sprinkler page 20 a-c dated July 8, 1996
(Added NYC Acceptance)
October 31, 1996
HORIZON® MIRAGE®
CONCEALED SPRINKLER
Follow instructions provided in
11 INSTALLATION II paragraph 7.
6. Place the system back in service
and secure all valves. Check the
replaced sprinklers and repair all
leaks.
E. Sprinkler systems that have been
subjected to a fire must be returned to
service as soon as possible. The en-
ti re system must be inspected for
damage and repaired or replaced as
necessary. Sprinklers that have been
exposed to corrosive products of
combustion or high ambient tempera-
tures, but have not operated, should
be replaced. Refer to the Authority
Having Jurisdiction for minimum re-
placement requirements.
Form No. 021993
February 15, 1996
1. PRODUCT NAME
Viking Model M
Extra Large Orifice Sprinkler
2. MANUFACTURER
THE VIKING CORPORATION
210 N. Industrial Park Road
Hastings, Michigan 49058 U.S.A.
Telephone: (616) 945-9501
( 800) 968-9501
Fax Number: (616) 945-9599
From outside U.S.A.
Telephone: + 1 (616) 945-9501
Fax Number: + 1 (616) 945-9599
3. PRODUCT DESCRIPTION
The Viking Model M Extra Large Orifice
Sprinkler is a thermo-sensitive glass-
bulb spray sprinkler. A rugged 5mm
glass-bulb, an extra large orifice, and the
familiar Model M design, are combined
in the standard response Model M Extra
Large Orifice Sprinkler.
The extra large orifice provides greater
flows at lower pressures than those pro-
duced by standard orifice or large orifice
sprinklers. This feature allows reduced
pipe sizing for hydraulically calculated
sprinkler systems which require high
densities of water. The Model M Extra
Large Orifice Sprinkler may eliminate
the need for a fire pump or reduce the
size of the pump if it is required. On
existing systems, replacing large orifice
sprinklers with extra large orifice sprin-
klers may provide the higher densities
required to allow an increase in the haz-
ard classification of an occupancy .
Viking Model M Extra Large Orifice
Sprinklers are available in both upright
and pendent styles with finishes and
temperature ratings to meet desiin re-
quirements. The special Teflon and
polyester coatings can be used in deco-
rative applications where colors are de-
sired. In addition, these two finishes are
corrosion resistant and provide protec-
tion against many corrosive environ-
ments.
During fire conditions, the heat sensitive
liquid in the glass-bulb expands, causing
the bulb to shatter, releasing the pip cap
and sealing spring assembly. The water
flowing through the sprinkler orifice
strikes the sprinkler deflector forming a
uniform spray pattern to extinguish or
control the fire.
Viking Model M Extra Large Orifice
Sprinklers may be ordered and/or used
as open sprinklers (glass-bulb and pip
cap assembly removed) on deluge sys-
tems.
TECHNICAL DATA
The Viking Model M Extra
Large Orifice Upright Sprinkler
is UL listed and FM Approved
for use in High Piled Storage
Occupancies.
See Approval Chart and Figure A.
When acceptable to the
Authority Having Jurisdiction,
Viking Model M Extra Large Orifice
Upright sprinklers may be used to
protect single, double, multiple-row,
and portable rack storage of Class
I-IV group A and B plastics, cartoned,
expanded or unexpanded, as well as
exposed unexpanded with:
a maximum storage height of
,. 20 ft. (6, 1 m),
a maximum ceiling height of
25 ft. (7,6 m),
36 inches (914,4 mm) minimum
deflector to top of storage
clearance,
design density of 0.60 gpm/sq. ft.
(24,5 I/min/sq. meter), and a
design area of
2000 sq. ft. (186 sq. meters)
for wet systems or
2600 sq. ft. (242 sq. meters),
for dry systems.
A~'i'\ oo~~prinkler 13 e
MODELM
EXTRA LARGE ORIFICE
SPRINKLER
Upright
4. TECHNICAL DATA
See Chart (page 13 g) for list of approvals.
Glass Bulb Fluid Temperature rated to
-65°F (-55°C)
Rated 175 PSI (1 207 kPa) water work-
ing pressure
Factory tested hydrostatically to 500 PSI
(3 448 kPa)
Thread size: 3/4 NPT (20mm)
Orifice Size: Nominal 5/8" (16mm)
K Factor: 11.5 (16,6 Metric for use when
pressure is measured in kPa)
Spring: USA Patent No. 4,167,974
Bulb: USA Patent No. 4,796,710
Spacing requirements: Refer to Ap-
proval Chart and Figure A
Minimum operating pressure require-
ments: Refer to to Approval Chart
and Figure A
Materials:
Frame: Brass castings UNS-C84400
Deflector: Brass UNS-C26000
Bulb: Glass; Nominal 5mm diameter
Seal: Teflon® Tape
Spring: Nickel Alloy
Sprinkler Nominal Sprinkler Ceiling Temperature at Sprinkler
Temperature Temperature Rating Max. Ambient Max. Recommend. Bulb
Classification (Fusing Point) Temp. Allowed1 Ambient Temp.2 Color3
Ordinary 135°F(57°C) 115°F(46°C) 100°F(38°C) Oranqe
Ordinarv 155°F(68°C) 135°F(57°C) 100°F(38°C) Red
Intermediate 175°F(79°C) 155°F(68°C) 150°F(65°C) Yellow
Intermediate 200°F(93°C) 180°F(82°C) 150°F(65°C) Green
High 286°F(141°C) 266°F(130°C) 225°F(107°C) Blue
Sprinkler Finishes: Brass, Polished Chrome, Black Teflon® and White Polyester.
Corrosion Resistant Coatings4: Black Teflon® and White Polyester in all temperatures and
Wax coated brass in the following temperatures:
135°F(57°C) White Wax 175°F(79°C) Dark Brown Wax
155°F(68°C) Light Brown Wax 200°F(93°C) Dark Brown Wax.
1 Based on National Fire Prevention and Control Administration Contract No. 7-34860.
2 Based on NFPA-13. Other limits may apply depending on fire loading, sprinkler location and other
authority having jurisdiction requirements. Refer to specific installation standards. 3 Temperature rating is stamped on deflector.
4 The Corrosion Resistant Coatings have passed the standard corrosion test required by the listed
approving agencies. These tests cannot and do not represent all possible corrosive environments. Prior
to installing, verify through the end user, that the coatings are compatible or suitable for the proposed
environment. The coatings indicated are applied to the exposed exterior surfaces inly and therefore
cannot be used as open sprinklers. Note that the spring is exposed on the Teflon coated sprinkler
and the White Polyester sprinkler.
Note: Units of measure in parentheses may be approximations.
Form No. 010692
Replaces Sprinkler page 13 e, f, & g dated April 1, 1994
(Added FM Approved upright ELO.)
Sprinkler 13 f February 15, 1996
MODELM
TECHNICAL DATA EXTRA LARGE ORIFICE
SPRINKLER
UL & ULC Spacing and Minimum Pressure Requirements*
Maximum Spacing {UL & C-UL Upright and UL & ULC Pendent)
Ordinary Hazard Occupancies (UL & C-UL Upright and UL & ULC Pendent):
130 Ft2 (12,0 m2)
Extra Hazard Occupancies (UL & C-UL Upright and UL & ULC Pendent):
90 Ft2 ( 8,4 m2) for pipe schedule systems.
100 Ft2 ( 9,3 m2) for systems hydraulically calculated according to NFPA 13 with densities of .25 GPM/Ft2 (10,2 Umin/m2)
or greater.
130 Ft2 ~ 12, 1 m2) for systems hydraulically calculated according to NFPA 13 with densities less than .25 GPM/Ft2 (10,2
Umin/m ).
High Piled Storage (UL & C-UL Upright):
100 Ft2 ( 9,3 m2) for systems hydraulically calculated according to NFPA 231, 231 C, or 231 D with densities of .25 GPM/Ft2
(10,2 Umin/m2) or greater.
130 Ft2 ( 1221 m2) for systems hydraulically calculated according to NFPA 231, 231 C, or 231 D with densities less than
.25 GPM/Ft (10,2 Umin/m2).
Maximum Distance Between Sprinklers {UL & C-UL Upright and UL & ULC Pendent)
Ordinary Hazard Occupancies (UL & C-UL Upright and UL & ULC Pendent):
15 Ft (4,6 m)
Extra Hazard Occupancies (UL & C-UL Upright and UL & ULC Pendent):
12 Ft (3,7 m) -Exception #1: Maximum distance between sprinklers= 12'-6" (3,8 m) in bays 25 ft. (7,6 m) wide.
Exception #2: Maximum distance between sprinklers= 15'-0" (4,6 m) for systems hydraulically
calculated according to NFPA 13 with densities less than .25 GPM/Ft2 (10,2 Umin/m2).
High Piled Storage Occupancies (UL & C-UL Upright):
12 Ft (3,7 m) -Exception #1: Maximum distance between sprinklers= 12'-6" (3,8 m) in bays 25 ft. (7,6 m) wide.
Exception #2: Maximum distance between sprinklers = 15'-0" (4,6 m) for systems hydraulically
calculated according to NFPA 13 with densities less than .25 GPM/Ft2 {10,2 Umin/m2).
Minimum Distance Between Sprinklers (UL & C-UL Upright and UL & ULC Pendent)
Ordinary Hazard & Extra Hazard (UL & C-UL Upright and UL & ULC Pendent)
6 Ft (1.8 m) -Unless provided with baffles installed according to NFPA 13
High Piled Storage Occupancies (UL & C-UL Upright only):
6 Ft (1.8 m) -Unless provided with baffles installed according to NFPA 13
Minimum Operating Pressure (UL & C-UL Upright and UL & ULC Pendent)
Ordinary Hazard & Extra Hazard (UL & C-UL Upright and UL & ULC Pendent)
7 PSI (48,3 kPa) _
High Piled Storage Occupancies (UL & C-UL Upright only):
10 PSI (70 kPa)
FM** Approval Spacing & Minimum Pressure Requirements
Maximum Spacing {FM Upright only)
Ordinary Hazard, Extra Hazard, and High Piled Storage Occupancies (FM Upright only):
100 Ft2 (9 ,3 m2)
Maximum Distance Between Sprinklers (FM Upright only)
Ordinary Hazard, Extra Hazard, and High Piled Storage Occupancies (FM Upright only):
12 Ft (3,7 m)
Minimum Distance Between Sprinklers (FM Upright only)
Ordinary Hazard, Extra Hazard, and High Piled Storage Occupancies (FM Upright only):
7 Ft (2,1 m)
Minimum Operating Pressure (FM Upright only)
Ordinary Hazard, Extra Hazard, and High Piled Storage Occupancies (FM Upright only):
10 PSI (70 kPa)
Figure A
Listing and Approval Spacing and Minimum Pressure Requirements Requirements
*UL, ULC, & C-UL listing of ELO Sprinklers requires installation to comply with recommendations set forth in NFPA Installation Standards. UL, ULC, & C-UL
spacing and minimum pressure requirements shown are taken from NFPA 13 (1994 ed.), 231 (1995 ed.), 231-C (1995 ed.), and 231-0 (1994 ed) and are provided
** for reference only. For FM Approval, installation must compy with requirements of applicable Factory Mutual Loss Prevention Data Sheets.
February 15, 1996
I
I
TECHNICAL DAT A
MODEL M 5mm GLASS BULB
STANDARD RESPONSE
EXTRA LARGE ORIFICE
Sprinkler 13 g
MODEL M
EXTRA LARGE ORIFICE
SPRINKLER
KEV ri:=== Temperature
r--Finish
A 1 X-Escutcheon (Pdt. Sprinkler only)
Thread Nominal Deflector Nominal Overall Approval 2
Size Orifice Style K Factor3 Length
UL4 ULC4 C-UL5 NYC6 FM7 N.P.T. B.S.P. Inches MM Description
3/4" 20mm 5/8" 16 Pendent
3/4" 20mm 5/8" 16 Upright
APPROVED TEMPERATURES
A -135°F (57°C), 155°F(68°CJ, 175°F ( 79°C),
200°F (93°C), 286°F (141 C)
B -135°F (57°C), 155°F(68°C), 175°F ( 79°C),
200°F (93°C)
C -286°F (141°C)
D -155°F(68°CJ, 175°F ( 79°C), 200°F (93°C), 286°F (141 C)
E -155°F(68°C), 175°F ( 79°C), 200°F (93°C)
Base P/N1 U.S. Metric Inches MM
A2.X A2.X
07961 11.5 16,6 2.75 69,9 B2Y B2Y
B4X B4X
D2 --
09679 11.5 16,6 2.75 69,9 E4 --cs --
APPROVED FINISHES
1 -Brass, Chrome
2 -Brass, Chrome, Black Teflon®· and White Polyester
3 -Brass, Chrome, and Black Teflon®
4 -Wax coated Brass. Corrosion Resistant
5 -Brass with 200°F (93°C) wax coating. (For corrosion
resistance.) Maximum ambient ceiling temperature
at ceiling= 150°F (65°C).
FOOTNOTES
--A3X --B3Y ----B4X
D2 --
E4 --D1 cs --
APPROVED ESCUTCHEONS
X -Standard (surface)
Y -Standard (surface) or
recessed with E-1
escutcheon
1 Base part number shown. For complete part number, see price list.
2 This Chart shows the listin~s and approvals available at the time of printing. Other approvals are in process. Check with the
manufacturer for any additional approvals.
3 Metric K Factor shown is for use when pressure is measured in kPa. When pressure is measured in BAR, multiply the
metric K Factor shown by 10.0.
4 For UL and ULC listing requirements concerning ELO sprinkler spacing and minimum pressure requirements, refer to Figure A and
applicable installation standards.
5 Listed by Underwriters Laboratories Inc. for use in Canada.
6 Accepted for use, City of New York Department of Buildings MEA 89-92-E Vol. III.
7 For FM Approval requirements concerning ELO sprinkler spacing and minimum pressure requirements, refer to Figure A. Also refer to
applicable FM Loss Prevention Data sheets.
Pintle Screw: Brass UNS-C36000.
Pip Caj: Copper UNS -C31600
Teflon Sprinklers:
Spring: Nickel Alloy; Exposed
Pintle Screw: Brass UNS-C36000
Tin plated, painted black for
appearance only
Pip Cap: Leaded Bronze
UNS-C31600
Teflon® coated
Polyester Sprinklers:
Spring: Nickel Alloy; Exposed
Pintle Screw: Brass UNS-C36000
Tin plated, painted white for
appearance only
Pip Cap: Leaded Bronze
UNS-C31600 ·
Tin plated
Accessories:
Sprinkler Wrench
Standard ELO wrench:
PN 07297M
Wrench for coated & recessed ELO
sprinklers:
PN 07565W/B (1 /2" ratchet required)
Available Finishes:
Chrome, Brass, Black Teflon® or
White Polyester
5. AVAILABILITY AND SERVICE
Viking sprinklers are available through a
network of Domestic, Canadian, and In-
ternational Distributors, see the Yellow
Pages of the telephone directory (listed
under "Sprinklers Automatic Fire") or
write to The Viking Corporation.
6. GUARANTEES
For details of warranty, refer to Viking's
current list price schedule or contact Vi-
king directly.
7. INSTALLATION
WARNING: Viking sprinklers are manu-
factured and tested to meet the rigid
requirements of the approving agency.
The sprinklers are designed to be in-
stalled in accordance with recognized
installation standards. Deviation from
the standards or any alteration to the
sprinkler after it leaves the factory in-
eluding, but not limited to, painting,
plating, coating or modification, may
render the sprinkler inoperative and will
automatically nullify the approval and
any guarantee made by The Viking Cor-
poration.
A. Sprinklers are to be installed in ac-
cordance with the latest published
standards of the National Fire Protec-
tion Association, Factory Mutual,
Loss Prevention Council, Assembles
Pleniere, Verband der Sachver-
sicherer or other similar organiza-
tions and also with the provisions of
governmental codes, ordinances and
standards whenever applicable. The
use of Extra Large Orifice sprinklers
may be limited due to occupancy and
hazard. Refer to the Authority Hav-
ing Jurisdiction prior to installation.
8. Sprinklers must be handled with care.
They must be stored in a cool, dry
place in their original shipping con-
tainer. Never install sprinklers that
have been dropped, damaged or ex-
posed to temperatures in excess of
•
Sprinkler 13 h
7/16" 1-3/4"
(11,1mm)
3/4"
(20mm) NPT
TECHNICAL DATA
t
2-3/4"
(69,9mm)
---::.·,·:•:~.:;:-./::~.:.1'··:·:'.tf•·'.,.
l
February 15, 1996
MODELM
EXTRA LARGE ORIFICE
SPRINKLER
3/4"
'-c2omm)
Model M NPT
7/16" ..... c11 , 1 mm) Model M Extra Large Orifice
Model M Pendent Sprinkler
Model M Extra Large Orifice
Pendent Sprinkler Extra Large Orifice
Upright Sprinkler Extra Large Orifice Installed with Model E-1 Installed with 1 /8" (3, 1 mm)
Escutcheon Pendent Sprinkler Recessed Escutcheon
the maximum ambient temperature
allowed. Never install any glass bulb
sprinkler if the bulb is cracked or if
there is a loss of liquid from the bulb.
(These sprinklers should be de-
stroyed immediately).
_C. Corrosion resistant sprinklers must
be installed when subject to corrosive
atmospheres. When installing corro-
sion resistant sprinklers, take care
not to damage the corrosion resistant
coating. Use only the special wrench
designed for installing coated Viking
sprinklers (any other wrench may
damage the unit).
Note: All dimensions are approximate.
Figure B
compound or tape applied and rein-
stalled. This is due to the fact that
when the joint seal is damaged, the
sealing compound or tape is washed
out of the joint. Air testing the sprin-
kler piping prior to testing with water
may be considered in areas where
leakage during testing must be pre-
vented. Refer to the Installation
Guides, and the Authority Having Ju-
risdiction.
F. Sprinklers must be protected from
mechanical damage. Wet pipe sys-
tems must be provided with adequate
heat. When installing Extra Large
Orifice Sprinklers on dry systems,
refer to the Installation Guides, and
the Authority Having Jurisdiction.
8. MAINTENANCE
D. The sprinkler must be installed after
the piping is in place to prevent me-
chanical damage. Before installing,
make sure the appropriate model,
style, orifice size and temperature rating are used. NOTICE: The owner is responsible for
1. Install escutcheon, (if used) which maintaining the fire protection system
is designed to thread on to the and devices in proper operating condi-
external threads of the sprinkler. tion. For minimum maintenance and in-
Refer to "Sprinkler Accessories" spection requirements, refer to the Na-
for approved escutcheons and tional Fire Protection Association Pam-
other accessories. phlet that describes care and mainte-
2. Apply a small amount of pipe joint nance of sprinkler systems. In addition,
compound or tape to the external the Authority Having Jurisdiction may
threads of the sprinkler only, tak-have additional maintenance, testing
ing care not to allow a build up of and inspection requirements which must
compound in the sprinkler inlet. be followed.
3. Install the sprinkler on the piping A. The Sprinklers must be inspected on
using the special sprinkler wrench a regular basis for corrosion, me-
anly, taking care not to over-chanical damage, obstructions,
tighten or damage the sprinkler paint, etc. The frequency of the in-
operating parts. DO NOT use the spections may vary due to corrosive
deflector to start or thread the atmospheres, water supplies and ac-
sprinkler into a fitting. tivity around the device.
E. After installation, the entire sprinkler 8. Sprinklers that have been painted or
system must be tested in accordance mechanically damaged must be re-
with the recognized installation placed immediately. Sprinklers
standards. The test is applied after showing signs of corrosion shall be
the sprinkler installation to insure no tested and/or replaced immediately
damage has occurred to the sprinkler as required. Standard response
during shipping and installation, and Sprinklers that are 50 years old shall
to make sure the sprinkler has been be tested and/or replaced as re-
properly tightened. If a thread leak quired. Sprinklers that have oper-
should occur, normally the sprinkler ated cannot be reassembled or re-
must be removed, new pipe joint used, but must be replaced. When
Replaces Sprinkler page 13 e, f, & g dated April 1, 1994
(Added FM Approved upright ELO.)
replacing sprinklers, use only new
sprinklers.
C. The sprinkler discharge pattern is
critical for proper fire protection,
therefore, nothing should b~ hung
from, attached to, or otherwise ob-
struct the discharge pattern. All ob-
structions must be immediately re-
moved or, if necessary, additional
sprinklers installed.
D. When replacing existing sprinklers,
the system must be removed from
service. Refer to the appropriate sys-
tem description and/or valve instruc-
tions. Prior to removing the system
from service, notify all Authorities
Having Jurisdiction. Consideration
should be given to employment of a
fire patrol in the affected area.
1. Remove the system from service,
draining all water and relieving all
pressure on the piping.
2. Using the special sprinkler wrench,
remove the old sprinkler and in-
stall the new unit. Care must be
taken to replace the sprinkler with
the proper model, style, orifice
size and temperature rating. A
fully stocked spare sprinkler cabi-
net should be provided for this
purpose.
3. Place the system back in service
and secure all valves. Check and
repair all leaks.
E. Sprinkler systems that have been
subjected to a fire must be returned
to service as soon as possible. The
entire system must be inspected for
damage and repaired or replaced as
necessary. Sprinklers that have
been exposed to corrosive products
of combustion or high ambient tem-
peratures, but have not operated,
should be replaced. Refer to the
Authority Having Jurisdiction for mini-
mum replacement requirements.
Form No. 010692
September 28, 1998
I TECHNICAL DATA
Upright Pendent Conventional
Viking Micromatic® Model M Sprinkler
Figure A
1. PRODUCT NAME
Viking Micromatic® Model M
Sprinkler
Styles: Upright, Pendent, and
-Conventional
Manufactured since 1997
2. MANUFACTURER
THE VIKING CORPORATION
210 N. Industrial Park Road
Hastings, Michigan 49058, U.S.A.
Telephone: (616) 945-9501
(877) 384-5464
Fax: (616) 945-9599
e-mail: techsvcs@vikingcorp.com
3. PRODUCT DESCRIPTION
The Viking Micromatic® Model M Sprin-
kler is a small, thermosensitive glass-
bulb spray sprinkler. The sprinkler is
available in several styles, finishes, tem-
perature ratings, and orifice sizes to
meet design requirements. The small
frame and rugged 5 mm glass bulb are
aesthetically pleasing. Used in conjunc-
tion with one of the various corrosion-re-
sistant coatings, the unit provides pro-
tection against many corrosive environ-
ments. In addition, the special polyester
or Teflon® coatings can also be used in
decorative applications where colors are
desired.
During fire conditions, the heat-sensitive
liquid in the glass bulb expands, causing
the bulb to shatter, releasing the pip cap
and sealing spring assembly. Water
flowing through the sprinkler orifice
strikes the sprinkler deflector, forming a
uniform spray pattern to extinguish or
control the fire.
4. TECHNICAL DATA
See Table 2 (page 11 c) and Table 3
(page 11 d) for list of approvals.
Maximum spacing: 15 ft. (4,57 m)
Minimum spacing: 6 ft (1,8 m)
Minimum operating pressure:
7 PSI (48,3 kPa)
Glass-bulb fluid temperature rated to
-65 °F (-55 °C)
Rated 175 PSI (1 207 kPa) water
working pressure
Factory tested hydrostatically to
500 PSI (3 448 kPa)
Spring: USA Patent No. 4,167,974
Materials:
Frame -Brass castings UNS-C84400
Deflector -Brass UNS-C26000
Bulb -Glass with glycerin solution;
Nominal 5 mm diameter
Seal -Teflon® tape
Spring -Nickel alloy
Screw -Brass UNS-C36000.
Pip Cap -Copper UNS-C11000
and Stainless Steel UNS-S30400
,-eflon® Sprinklers:
Spring -Nickel alloy, exposed
Screw -Brass UNS-C36000
Pip Cap -Copper UNS-C11000 and
Stainless Steel UNS-S30400;
Teflon® coated
Polyester Sprinklers:
Spring -Nickel alloy, exposed
Screw -Brass UNS-C36000
Pip Cap -Copper UNS-C11000
and Stainless Steel UNS-S30400
Accessories:
Sprinkler Wrench
Standard Micromatic® Wrench:
Part No. 05000CM
Wrench for coated and recessed
sprinklers:
Part No. 07398W
Refer to "Sprinkler Accessories" for
other accessories.
MICROMATIC®
MODELM
SPRINKLER
Available Finishes:
Chrome-Enloy® (patents pending),
Brass, Bright Brass, White Polyester,
Black Polyester, Black Teflon®, or
Wax-Coated Brass or Polyester
5. AVAILABILITY AND SERVICE
Viking sprinklers are available through
a network of domestic, Canadian, and
international distributors. See the Yel-
low Pages of the telephone directory
for a local distributor (listed under
"Sprinklers-Automatic-Fire") or contact
The Viking Corporation.
Viking Technical Data may be found on
The Viking Corporation's Web site at
http://www.vikingcorp.com.
The Web site may include a more recent
edition of this Technical Data page.
6. GUARANTEES
For details of warranty, refer to Viking's
current price schedule, or contact The
Viking Corporation directly.
7. INSTALLATION
WARNING: Viking sprinklers are manu-
factured and tested to meet the rigid
requirements of the approving agency.
The sprinklers are designed to be in-
stalled in accordance with recognized
installation standards. Deviation from
the standards or any alteration to the
sprinkler after it leaves the factory in-
cluding, but not limited to, painting, plat-
ing, coating, or modification, may render
the sprinkler inoperative and will auto-
matically nullify the approval and any
guarantee made by The Viking Corpora-
tion.
A. Sprinklers are to be installed in ac-
cordance with the latest published
standards of the National Fire Protec-
tion Association, Factory Mutual,
Loss Prevention Council, Assemblee
Pleniere, Verband der Sachver-
sicherer or other similar organiza-
tions, and also with the provisions of
governmental codes, ordinances,
and standards whenever applicable.
B. Sprinklers must be handled with care.
They must be stored in a cool, dry
place in their original shipping con-
tainer. Never install sprinklers that
have been dropped, damaged, or ex-
posed to temperatures in excess of
the maximum ambient temperature
allowed. Never install any glass-bulb
sprinkler if the bulb is cracked or if
there is a loss of liquid from the bulb.
If a glass bulb lacks the appropriate
amount of fluid, it should be set aside
Note: Units of measure in parentheses may be approximations.
Form No. F _ 100397
Replaces page 13 a-d and page 11 a-d, dated
August 3, 1998 (updated list of approvals).
Sprinkler 11 b
TECHNICAL DATA
Sprinkler Nominal Sprinkler Ceiling Temperature at Sprinkler Bulb Temperature Temperature Rating Max. Ambient Max. Recommended Color3 Classification (Fusing Point) Temp. Allowed1 Ambient Temp.2
Ordinary 135 °F (57 °C) 115 °F (46 °C) 100 °F (38 °C) Orange
Ordinarv 155 °F (68 °C} 135 °F (57 °C} 100 °F (38 °C) Red
Intermediate 175 °F (79 °C) 155 °F (68 °C) 150 °F (65 °C) Yellow
I nter_mediate 200 °F (93 °C) 180 °F (82 °C) 150 °F (65 °C) Green
Intermediate 212 °F (100 °C) 192 °F (88 °C) 150 °F (65 °C) Green
High 286 °F (141 °C) 266 °F (130 °C) 225 °F (107 °C) Blue
Extra High 360 °F (182 °C) 340 °F (171 °C) 300 °F (149 °C) Mauve
Ultra High5 500 °F (260 °C) 480 °F (249 °C) 465 °F (240 °C) Black
Sprinkler Finishes: Brass, Bright Brass, Chrome-Enloy®, White Polyester,
Black Polyester, and Black Teflon®
Corrosion-Resistant Coatlngs4: Polyester and Teflon® in all temperatures,
Wax-Coated Brass, and Wax over Polyester in the following temperatures:
135 °F (57 °C) White Wax 175 °F (79 °C) Dark Brown Wax
155 °F (68 °C) Light Brown Wax 200 °F (93 °C) Dark Brown Wax
212 °F (100 °C) Dark Brown Wax
FOOTNOTES
1 Based on National Fire Prevention and Control Administration Contract No. 7-34860. 2 Based on NFPA-13. Other limits may apply depending on fire loading, sprinkler location, and other
Authority-Having-Jurisdiction requirements. Refer to specific installation standards .
... 3 Temperature rating is stamped on the deflector. 4 The corrosion-resistant coatings have passed the standard corrosion test required by the listed
approving agencies. These tests cannot and do not represent all possible corrosive environments.
Prior to installing, verify through the end user that the coatings are compatible or suitable for the
proposed environment. The coatings indicated are applied to the exposed exterior surfaces only and,
therefore, cannot be used as open sprinklers. Note that the spring is exposed on the Teflon®-coated
sprinkler and the White Polyester sprinkler. 5 Sprinklers of Ultra High temperature rating are intended for use inside ovens, dryers, or similar
enclosures with normal operating temperatures above 300 °F (149 °C). Where the ambient temperature
around the_ Ultra High temperature rated sprinkler is significantly reduced below 300 °F (149 °C),
response time of the Ultra High temperature rated sprinkler may be severely retarded.
Table 1
and returned to Viking (or an author-
ized Viking distributor) for analysis as
soon as possible. If the sprinkler is
not returned to Viking, it should be
destroyed immediately.
C. Corrosion-resistant sprinklers must
be installed when subject to corrosive
atmospheres. When installing corro-
sion-resistant sprinklers, care must
be taken not to damage the corro-
sion-resistant coating. Use only the
special sprinkler wrench and immedi-
ately replace any damaged units.
D. Before installation, be sure to have
the appropriate sprinkler model and
style, with the proper orifice size,
temperature rating, and response
characteristics. The sprinklers must
be installed after the piping is in place
to prevent mechanical damage.
1. Install escutcheon (if used), which
is designed.to thread onto the ex-
ternal threads of the sprinkler.
When installing sprinklers using a
Model E-1 or Model F-1 Escutch-
eon, thread the center adapter
ring onto the external threads of
the sprinkler. Refer to the 11Sprin_-
kler Accessories" section of the
Viking Engineering and Design
Data book for approved escutch-
eons and other accessories.
2. Apply a small amount of pipe-joint
compound or tape to the external
threads only, taking care not to
allow a build-up of compound in
the sprinkler orifice.
.. 3. Install the sprinkler on the piping
using the special sprinkler wrench
only, while taking care not to dam-
age the sprinkler operating parts.
(Any other type of wrench may
damage the unit). DO NOT use
the sprinkler deflector to start or
thread the sprinkler into a fitting.
E. After installation, the entire sprinkler
system must be tested in accordance
with the recognized installation
standards. The test is applied after
sprinkler installation to ensure that no
damage has occurred to the sprinkler
during shipping and installation, and
to make sure the unit has been prop-
erly tightened. If a thread leak should
occur, normally the sprinkler must be
removed, new pipe-joint compound
or tape applied, and then reinstalled.
This is due to the fact that when the
joint seal is damaged, the sealing
compound or tape is washed out of
September 28, 1_998
MICROMATIC®
MODELM
SPRINKLER
the joint. Air testing the sprinkler pip-
ing prior to testing with water may be
considered in areas where leakage
during testing must be prevented.
Refer to to the Installation Guides and
the Authority Having Jurisdiction.
F. Sprinklers must be protected from
mechanical damage. Wet pipe sys-
tems must be provided with adequate
heat. When installing sprinklers on
dry systems, refer to the Installation
Guides and the Authority Having
Jurisdiction.
8. MAINTENANCE
NOTICE: The owner is responsible for
maintaining the fire-protection system
and devices in proper operating condi-
tion. For minimum maintenance and in-
spection requirements, refer to the Na-
tional Fire Protection Association pam-
phlet that describes care and mainte-
nance of sprinkler systems. In addition,
the Authority Having Jurisdiction may
have additional maintenance, testing,
and inspection requirements which must
be followed.
A. Sprinklers must be inspected on a
regular basis for corrosion, mechani-
cal damage, obstructions, paint, etc.
The frequency of the inspections may
vary due to corrosive atmospheres,
water supplies, and activity around
the device.
B. Sprinklers that have been painted or
mechanically damaged must be re-
placed immediately. Sprinklers
showing signs of corrosion shall be
tested and/or replaced immediately
as required. Micromatic® Model M
Sprinklers that are 50 years old shall
be tested and/or replaced as re-
quired. Sprinklers that have operated
cannot be reassembled or re-used,
but must be replaced. When replac-
ing sprinklers, use only new sprin-
klers.
C. The sprinkler discharge pattern is
critical for proper fire protection.
Therefore, nothing should be hung
from, attached to, or otherwise ob-
struct the discharge pattern. All ob-
structions must be immediately re-
moved or, if necessary, additional
sprinklers installed.
D. When replacing existing sprinklers,
the system must be removed from
service. Refer to the appropriate sys-
tem description and/or valve instruc-
tions. Prior to removing the system
from service, notify all Authorities
Having Jurisdiction. Consideration
should be given to employment of a
fire patrol in the affected area.
(continued on page 11 d)
...,_
September 28, 1998 Sprinkler 11 c
TECHNICAL DATA
I
MICROMATIC®
MODELM
SPRINKLER
MICROMATIC® MODEL M SPRINKLER
5 mm GLASS BULB, STANDARD RESPONSE See row A KEY See row 3 of
of Approved -i r-Approved
STANDARD ORIFICE Temp. Chart A 3 Finish Chart
Thread Nominal Deflector Nominal Overall Approvals2 Size Orifice s le K-Factor6 Len th
N.P.T. B.S.P. lnche Base P/N1 U.S. Metric Inches mm UL C-UL FM NYC3 VdS LPCB
1/2" 1/2 10138 5.5 2.3 --A3 84 C6 F7 A3 84 C6 F7 A7 D5 F7 A3 84 C6 --
1/2" 1/2 10139 5.5 2.3 --A3 84 C6 F7 A3 84 C6 F7 A7 D5 F7 A3 84 C6 A2 A1 B
1/2" 1/2 10233 5.5 2.3 58 A7 D5 F7 A2 A1 88
15 mm 15 10173 79 58 A3 84 C6 A3 84 C6 A7 D5 E1
15mm 15 10174 79 58 A7 D5 E1 A2 A1 88
15mm 15 10193 79 58 A3 84 C6 F7 A3 84 C6 F7 A7 D5 E1 A3 84 C6 --
LARGE ORIFICE
1/2" 17/32 --10220 8.0 2.4 61 A3 84 C6 F7 A3 84 C6 F7 A7 D5 F7 A3 84
1/2" 17/32 --4 10223 8.0 11 5 2.4 61 A3 84 C6 F7 A3 84 C6 F7 A7 D5 F7 A3 84
3/4" 17/32 --10141 8.0 11,5 2.4 61 A3,84,C6,F7 A3, 84, C6, F7 A7,D5,F7 A3,84,C6 A2 A1, 88
3/4" 17/32 --Pendent4 10142 8.0 11 5 2.4 61 A3 84 C6 F7 A3 84 C6 F7 A7 D5 F7 A3 84 C6 A2 1 88
15mm 20 Pendent4 10187 --A3 84 C6 F7 A3 84 C6 F7 D5 --A1 88
15mm 20 U ri ht 10190 --A3 84 C6 F7 A3 84 C6 F7 D5 --A1 88
20mm 20 U ri ht 10169 8.0 11,5 2.4 61 A3,B4,C6 A3,B4,C6 D5, E1 A2 A1,88
20mm 20 Pendent4 10170 8.0 11 5 2.4 61 A3 84 C6 A3 84 C6 D5 E1 A2 A1 88
SMALL ORIFICE
7/16 · U ri ht 10191 58 A3 84 C6 F7 A3 84 C6 F7
1/2" 3/8 U ri ht 10218 2.7 2.3 --A3,B4,C6,F7 A3, 84, C6, F7 A7,D5 A3,84
1/2" 7/16 --U ri ht 10219 4.0 2.3 --A3, 84, C6, F7 A3, 84, C6, F7 A3,84
1/2" 3/8 Pendent4 10221 2.7 2.3 58 A3 84 C6 F7 A3 84 C6 F7 A7 D5 A3 84
1/2" 7/16 --Pendent4 10222 4.0 58 A3,84,C6,F7 A3, 84, C6, F7 A3,B4
10mm 10 Pendent4 10175 58 2.3 58 A2 A1 B
10mm 10 U ri ht 10176 5,8 2.3 58 A2 A1 ,88
15mm ~8 U ri ht 10192 58 A3 84 C6 F7 A3 84 C6 F7 E5
15 mm 7/16 Pendent4 10188 --A3 84 C6 F7 A3 84 C6 F7
15mm 3/8 Pendent4 10189 --A3 84 C6 F7 A3 84 C6 F7
CONVENTIONAL
1/2" 1/2 Conv. 10227 5.5 2.3 A3, 84, C6 A3,B4,C6 A2 A1, 88
3/4" 17/32 --Conv. 10228 8.0 2.4 A3 84 C6 A3 84 C6 A2 A1 88
15 mm 15 Conv. 10172 7,9 58 A3, 84, C6 A3,84,C6 A2 A1 , 88
20 mm 20 Conv. 10168 11,5 61 A3, 84, C6 A3,84,C6 A2 A1, 88
APPROVED TEMPERATURES APPROVED FINISHES
A -135 °F (57 °C), 155 °F (68 °C), 175 °F (79 °C), 200 °F (93 °C), 1 -Brass, Bright Brass, and Chrome-Enloy® 286 °F (141 °C), and 360 °F (182 °C)
B -135 °F (57 °C), 155 °F (68 °C), 175 °F (79 °C), and 200 °F (93 °C)
C -286 °F (141 °C)
2 -Brass, Bright Brass, Chrome-Enloy®, White Polyester>,
and Black Polyesters
3 -Brass, Bright Brass, Chrome-Enloy®, Black Teflon®s,
White Polyesters, and Black Polyester>
D -135 °F (57 °C), 155 °F (68 °C), 175 °F (79 °C),
200 °F (93 °C), and 212 °F (100 °C)
E -135 °F (57 °C), 155 °F (68 °C), 175 °F (79 °C),
200 °F (93 °C), 212 °F (100 °C), 286 °F (141 °C), and 360 °F (182 °C)
F -500 °F (260 °C)7
4 -Wax-Coated Brass and Wax over Polyester
(corrosion resistant)
5 -Wax-Coated Brass (corrosion resistant)
6 -200 °F (93 °C) Wax Coating (corrosion resistant);
maximum ambient temperature allowed at
ceiling = 150 °F (65 °C)
7 -Brass and Chrome-Enloy®
8 -Wax-Coated Brass, Wax Over Polyester, White
Polyester, Black Polyester, and Black Teflon
FOOTNOTES
1 Base part number shown. For complete part number, refer to price list. 2 This table shows the listings and approvals available at the time of printing. Other approvals are in process. Check with the manufacturer
for any additional approvals. 3 Approved by the New York City Board of Standards and Appeals, MEA No. 89-92-E, Volume 12. 4 Refer to "Sprinkler Accessories" section for approved escutcheons and other accessories. 5 UL and C-UL approved as a corrosion-resistant sprinkler. 6 Metric K-Factor shown is for use when pressure is measured in kPa. When pressure is measured in BAR, multiply the metric K-Factor
shown by 10.0.
7 Sprinklers of Ultra High temperature rating are intended for use inside ovens, dryers, or similar enclosures with normal operating
temperatures above 300 °F (149 °C). Where the ambient temperature around the Ultra High temperature rated sprinkler is significantly
reduced below 300 °F (149 °C), response time of the Ultra High temperature rated sprinkler may be severely retarded.
Table 2
•
Sprinkler 11 d
TECHNICAL DATA
MICROMATIC® MODEL M SPRINKLER
5 mm GLASS BULB, STANDARD RESPONSE
September 28, 1998
MICROMATIC®
MODELM
SPRINKLER
KEY See row A ~ i---See row 3 of
of Approved Approved
INSTALLED WITH E-1 RECESSED ESCUTCHEON7 Temp. Chart A 3 Finish Chart
Thread Nominal Deflector Nominal Overall Approvals2 Size Orifice Style K-Factor8 Length
N.P.T. B.S.P. Inches mm Description Base P/N1 U.S. Metric Inches mm UL C-UL FM7 NYC3 VdS LPCB
1/2" --1/2 --Pendent4 10139 5.5 --2.3 --83 83 D1 83 82 83
3/4" --17/32 --Pendent4 10142 8.0 --2.4 --83 83 D1 83 82 83
--15 mm --15 Pendent4 10173 --7,9 --58 83 83 D1 --82 83
--20mm --20 Pendent4 10170 --11,5 --61 83 83 D1 --82 83
INSTALLED WITH F-1 ADJUSTABLE ESCUTCHEON6
1/2" --1/2 --Pendent4 10139 5.5 --2.3 --83 83 --83 C1 83
3/4" --17/32 --Pendent4 10142 8.0 --2.4 --83 83 --83 C1 83
--15mm --15 Pendent4 10173 --7,9 --58 --------C1 83
--20mm --20 Pendent4 10170 --11,5 --61 --------C1 83
~
APPROVED TEMPERATURES APPROVED FINISHES
A -135 °f (57 °C), 155 °F (68 °C), 175 °F (79 °C), 1 -Brass, Bright Brass, and Chrome-Enloy®
200 °F (93 °C), 286 °F (141 °C), and 360 °F (182 °C) 2 -Brass, Bright Brass, Chrome-Enloy®, White Polyester5, and Black Polyester5
B -135 °F (57 °C), 155 °F (68 °C}, 175 °F (79 °C), 3 -Brass, Bright Brass, Chrome-Enloy®, Black Teflon®5, White Polyester5,
and 200 °F (93 °C) and Black Polyester5
C -286 °F (141 °C) 4 -Wax-Coated Brass and Wax over Polyester (corrosion resistant)
5 -Wax-Coated Brass (corrosion resistant)
D -135 °F (57 °C}, 155 °F (68 °C), 175 °F (79 °C}, 6 -200 °f (93 °C) Wax Coating (corrosion resistant); maximum ambient
200 °F (93 °C}, and 212 °F (100 °C) temperature allowed at ceiling = 150 °F (65 °C)
FOOTNOTES
1 Base part number shown. For complete part number, refer to price list. 2 This table shows the listings and approvals available at the time of printing. Other approvals are in process. Check with manufacturer for any
additional approvals. 3 Approved by the New York City Board of Standards and Appeals, MEA No. 89-92-E, Volume 12. 4 Refer to "Sprinkler Accessories" section for approved escutcheons and other accessories. 5 UL and C-UL approved as a corrosion-resistant sprinkler. 6 E-1 Recessed Escutcheons and F-1 Adjustable Escutcheons must be ordered separately from sprinklers. Refer to the price list. 7 FM approval of recessed standard orifice and large orifice Model M pendent sprinklers with the E-1 Escutcheon is limited to Wet Systems and
Preaction Systems qualifying as Wet Systems, for hazard occupancies up to and including Ordinary Hazard Group II. 8 Metric K-Factor shown is for use when pressure is measured in kPa. When pressure is measured in BAR, multiply the metric K-Factor shown
by 10.0.
Table 3
1 . Remove the system from service,
drain all water, and relieve all
pressure on the piping.
2. Using the special sprinkler wrench,
remove the old sprinkler and in-
stall the new unit. Care must be
taken to ensure that the replace-
ment sprinkler is the proper model
and style, and has the appropriate
orifice size, temperature rating,
and response characteristics. A
fully stocked spare sprinkler cabi-
net should be provided for this
purpose.
3. Place the system back in service
and secure all valves. Check and
repair all leaks.
E. Sprinkler systems that have been
subjected to a fire must be returned
to service as soon as possible. The
entire system must be inspected for
damage, and repaired or replaced as
necessary. Sprinklers that have been
exposed to corrosive products of
combustion or high ambient tempera-
tures, but have not operated, should
be replaced. Refer to the Authority
Having Jurisdiction for minimum
replacement requirements.
Replaces page 13 a-d and page 11 a-d, dated
August 3, 1998 (updated list of approvals). Form No. F _ 100397