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HomeMy WebLinkAbout6021 INNOVATION WAY; ; FPC2017-0116; Permitity of PERMIT REPORT S Carlsbad Print Date: 10/20/2021 Permit No: FPC2017-0116 Job Address: 6021- 6023 INNOVATION WAY, CARLSBAD, CA 92009-1741 Status: Closed - Finaled Permit Type: FIRE-Construction Commercial Work Class: Underground Fire Parcel #: Track U: Applied: 05/05/2017 Valuation: $0.00 Lot U: Issued: 08/14/2017 Occupancy Group: Project U: Finaled Close Out: 08/12/2021 #of Dwelling Units: Plan U: Bedrooms: Construction Type: Bathrooms: Orig. Plan Check U: Inspector: Plan Check U: Final Inspection: Project Title: Description: BRESSI RANCH LOT 23 UNDERGROUND (REVISED) Applicant: INLAND VALLEY PIPELINE-DO NOT USE 27852 KELLER RD MENIFEE, CA 92584-9645 (951) 368-3903 FEE AMOUNT FIRE Expedited Plan Review Per Hour - Office Hours $132.00 FIRE Underground Piping with 5+ Hyds/Risers $996.00 Total Fees: $1,128.00 Total Payments To Date: $1,128.00 Balance Due: $0.00 Fire Department Page 1 of 1 1635 Faraday Avenue, Carlsbad CA 92008-7314 1 760-602-4665 1 760-602-8561 f I www.carlsbadca.gov EXCEL ENGINEERING LEVIN & DEN TINO INC. D.B.A. EXCEL ENGINEERING 440 State Place • Escondido, CA 92029 • (760)745-8118 • Fax 745-1890 • www.excelengineering.net Plan Revision Private Improvement Plans for: Bressi Ranch Lot 23 (Innovation Way) Date: 9/12/2017 SUMMARY OF REVISIONS: 1. The specifications for the P.V.C. for the fire lines servicing the site have been changed. The 8" and 10" lines servicing the hydrants have been changed from DR14 to DR18. The fire lines leading to the building are to remain DR 14. I U I I I I I I I I I I U I I I I I 1 FIRE FLOW ANALYSIS FOR: BRESSI RANCH LOT 23 INNOVATION WAY CARLSBAD Prepared For: RAF GROUP BRESSI RANCH LIC AUN: ADAM ROBINSON Prepared By: ENGINEERING LAND PLANNING ENGINEERING SURVEYING 440 STATE PLACE, ESCONDIDU, CA 92029 PH (760)745.8118 FX (760)745.1890 Excel Reference No.: 16-038 Date: May 2, 2017 I I PURPOSE/PROJECT DESCRIPTION I This water system analysis was conducted to check the capacities of the proposed onsite private underground fire distribution system and potable water supply lines that will serve the proposed Bressi Ranch Lot 23. A 12" lateral Polyvinyl chloride (PVC) connection will service the onsite fire system, originating from an existing 12" water line running below Innovation Way. The fire line connection will utilize an 8" double detector check valve (DDCV). The connection services an onsite fire system consisting of a 10" and 8" line that will serve the fire sprinklers and three separate hydrants around the site. CRITERIA AND METHODOLOGY The modeling of the onsite fire service lines was completed using the EPANET 2.0 program I (EPANET). Usage of the water and sewer plans provided the scaled distances for the project. The schematic used in EPANET can be found on Attachment 1. Head Loss Across Fittings Minor losses encountered in the Ductile Iron Pipe (DIP) fittings along the pipelines were I neglected in the model (i.e. elbows, tees, etc.). The headloss (HL) across the backflow apparatus was addressed and modeled using the method described below. The Watts 8" double check detector assembly (DCDA) was modeled as a general purpose valve (GPV) in series with a check valve. The HL curve can be found on the specification sheet for the Watts DCDA on Attachment 2. This information was used to develop Figure 1 below, which displays the HL curve created for usage in EPANET to model the flow within the system. Additional information for the proposed backflow device can be found on Attachment 2. I I I I I I I I I I I I I I I I I I I I I I I I I I Curve Editor Curve ID Description Ii JWattsDDCV8" Curve Type Equation IHEADL0SS j I Flow Headloss 24- 0 11.533 500 6.920 18- 16- 1000 8.073 E 14- 1500 11.533 10- 2000 18.453 0 1,000 2,00G 2500 24.22 Flow (GPM)________________ Load... Save... ] OK_J Cancel] help Fig. 1: HL Curve for the 8" DCDA Roughness Coefficients A Hazen-Williams roughness coefficient value of 150 was used for the PVC pipes in the system. Modeled Demand Flows To ensure the onsite hydraulics can supply adequate flow to the system during a fire event, Excel Engineering tested a primary and secondary scenario. The 2016 California Fire Code (CFC) refers to Appendix B to obtain fire-flow requirements for buildings. Using Table B105.1, it was determined that the larger, Type IlIB building would require a fire-flow of 3,500 gallons per minute (gpm). By providing the building with fire sprinklers, the required flow can be reduced by 75 percent and results in a required flow of 875 gpm. For the purposes of this report, the flow was only reduced by 50 percent. The calculated fire-flow system criteria enabled the following scenarios to be tested: Scenario 1 - For this scenario, a demand of 1,750 gpm was supplied to the system and distributed between two onsite hydrants, and no flow was provided to the building. Scenario 2 - For this scenario, a demand of 1,750 gpm was supplied to the system and distributed between two onsite hydrants, and a flow of 250 gpm was provided to the building. Tie-In Pressures Available Existing flow and pressure data from the public system in Innovation Way was taken from a flow analysis performed by the City of Carlsbad Fire Department (CCFD) on 09/24/2015. To model this scenario in EPANET the pressure available was modeled as a reservoir with a total head 2 I I I I I I I I I I I I I I I I I I I ( equivalent to the static pressures given in the analysis provided by the CCFD. This pressure test data can be found on Attachment 3 to this report, and is summarized in the table below. Table 1: CCFD Flow Test Results Hydrant NO Static Static Elevation (ft) Total Head Reservoir Pressure (psi) Pressure Available Number (ft of head) (ft) H20918 74 170.2 379 549.2 1 CALCULATONS AND CONCLUSIONS This performed analysis confirms that the underground fire distribution system will be adequate to provide fire flows to the site for Scenario 1 in accordance with the following requirements: Minimum residual pressure for the project shall be 20 pounds per square inch (psi) during fire flow demand. Pipe velocities shall not exceed 10 feet per second (fps). The velocity and pressure requirements were met for this project. Scenario 1 For this scenario, the highest velocity found in the system was in multiple pipes. This velocity was recorded as 7.15 fps. See Attachment 4. Minimum Pressure -For this scenario, the minimum pressure in the system is found in Junction 11. The recorded pressure was 57.75 psi. See Attachment 5. A velocity of 11.35 fps was found in the pipes leading to the hydrants (Pipe 10) for this scenario. Scenario 2 For this scenario, the highest velocity found in the system was in multiple pipes. This velocity was recorded as 8.17 fps. See Attachment 6. Minimum Pressure -For this scenario, the minimum pressure in the system is found in Junction 11. The recorded pressure was 53.55 psi. See Attachment 7. A velocity of 11.35 fps was found in the pipe leading to the hydrants (Pipe 10) for this scenario. 3 I I I I I I I I I I I I I I I I I Attachment I - Site Schematic ............... Junction #11 f250 gpm to this con nection (scenario 2) Junction #6 _1,000 gpm to this hydrant (both scenarios) Li 3- . Junction #24 / 750 gpm to this hydrant (both scenarios) I I I I I I Li] 757DCDABFG I I I 11 Attachment 2 - WATTS Specification Sheet S-757DCDA/757NDCDA For Non-Health Hazard Applications Job Name ______________________________________ Contractor Job Location Approval I Engineer Contractor's P.O. No. Approval Representative I Series 757DCDA, 757NDCDA Double Check Detector Assemblies are used to prevent backflow of non-health hazard pollutants that are objectionable but not toxic, from entering the potable water supply system. The 757DCDA, 757NDCDA may be installed under continuous pressure service and may be subjected to backpressure and backsiphonage. Series 757DCDA, 757NDCDA is used primarily on fire line sprinkler systems when it is necessary to monitor unauthorized use of water. Features Extremely compact design 70% Lighter than traditional designs 304 (Schedule 40) stainless steel housing & sleeve Groove fittings allow integral pipeline adjustment Patented tn-link spring check provides lowest pressure loss Unmatched ease of serviceability Available with grooved butterfly valve shutoffs May be used for horizontal, vertical or N pattern installations Replaceable check disc rubber Specifications The Double Check Detector Assembly shall consist of two independent tn-link check modules within a single housing, sleeve access port, four test cocks and two drip tight shutoff valves. Tr-link checks shall be removable and serviceable, with- out the use of special tools. The housing shall be constructed of 304 Schedule 40 stainless steel pipe with groove end con- nections. Tr-link checks shall have reversible elastomer discs and in operation shall produce drip tight closure against reverse flow caused by backpressure or backsiphonage. The bypass assembly shall consist of a meter, which registers in either gal- lon or cubic measurement, a double check backfiow assem- bly and required test cocks. Assembly shall be a Watts Series 757DCDA, 757NDCDA. I The information contained herein is not intended to replace the full product installation and safety information available or the experience of a trained product installer. You are required to thoroughly read all installation instructions and product safety information before beginning the installation of this product. Watts product specifications in U.S. customary units and metric are approximate and are provided for reference only. For precise measurements, please contact Watts TechnicalService. Watts reserves the right to change or modify product design, construction, specifications, or materials with- out prior notice and without incurring any obligation to make such changes and modifications on Watts products previously or subsequently sold. XVWATM 757DCDAOSY 757NDCDAOSY Series 757DCDA, 757NDCDA Double Check Detector Assemblies Sizes: 2½" -10(65-250mm) I I Dimensions - Weight ®0 C ® US c®us 1048 B64.5 Approved (°BFG & OSY Only) 757DCDABFG, 757NOCDABFG I I I I I I I I I I I I I I I I I I I Attachment 2 - WATTS Specification Sheet Available Models Suffix: OSY - UL/FM outside stem and yoke resilient seated gate valves BFG - UL/FM grooved gear operated butterfly valves with tamper switch *y FxG - Flanged inlet gate connection and grooved outlet gate connection *y GxF - Grooved inlet gate connection and flanged outlet gate connection *y GxG - Grooved inlet gate connection and grooved outlet gate connection Available with grooved NRS gate valves - consult factory* Post indicator plate and operating nut available - consult factory* *Consult factory for dimensions open) __A — - 757DCDA, 757NDCOA ti1U11I DIMENSIONS WEIGHT in. mm A in. mm C(OSY) in. mm D in. mm G in. mm H in. mm I In. mm J in. mm P in. mm 757DCDA lbs. kgs 757NDCDA lbs. kgs. 21/2 65 3Q3/4 781 16% 416 3½ 89 29'A6 738 21½ 546 15½ 393 813A6 223 13/16 335 139 63 147 67 _3 80 31% 806 18/8 479 3A6 94 30'/4 768 221/4 565 171/8 435 93A6 233 141/2 368 159 72 172 78 4 100 33% 857 22% 578 4 102 33 838 231h 597 18½ 470 915A6 252 153A6 386 175 79 198 90 _6 150 1 431h 1105 1 301A 765 5½ 140 443/4 1137 331/4 845 23/l6 589 1 13'A6 332 1 19 483 309 140 1 350 159 8 200 1 493/4 1264 373/4 959 1 611/6 170 541% 1375 1 401A 1019 277As 697 1 1511/16 399 1 213As 538 1 494 224 1 569 258 10 250 1 573% 1467 1 453/4 1162 1 8/io 208 66 1676 1 491h 1257 321h 826 1 17/i 440 1 24 610 1 795 361 1 965 438 iL4.1U11I DIMENSIONS WEIG in. mm A in. mm C in. mm D in. mm G in. mm in. H mm I in. mm J in. mm P in. mm 757DCDABFG lbs kgs 757NDcOABFG lbs. kgs. 21/2 65 273/4 705 8 203 31/2 89 297/8 759 211/2 546 14's/is 379 83'i6 223 13 330 70 32 78 35 3 80 281/4 718 8Vis 211 3"A6 94 301'A6 779 221/4 565 157As 392 93'i6 233 131/2 343 68 31 81 37 4 100 29 737 815/is 227 3"A6 94 31'5A6 811 231/2 597 161% 412 91% 252 14 356 75 34 98 44 6 150 1 361/2 927 10 254 1 5 127 1 433A6 1097 1 331/4 845 1 1911A6 500 1 131/is 332 1 141/2 368 1 131 59 171 78 8 200 1 423/4 1086 121/4 311 1 61/2 165 1 51'A6 1297 1 401/a 1019 1 235/is 592 1 15A6 399 1 183A6 462 1275 125 351 159 Noryl® is a registered trademark of General Electric Company. Materials Housing & Sleeve: 304 (Schedule 40) Stainless Steel Elastomers: EPDM, Silicone and Buna-N Tr-link Checks: Noryl®, Stainless Steel Check Discs: Reversible Silicone or EPDM Test Cocks: Bronze Body Nickel Plated Pins & Fasteners: 300 Series Stainless Steel Springs: Stainless Steel Pressure - Temperature Temperature Range: 33°F - 140°F (0.500 - 60°C) Maximum Working Pressure: 175p5i (12.1 bar) Approvals - Standards Approved by the Foundation for Cross-Connection Control and Hydraulic Research at The University of Southern California (FCCCHR-USC) Attachment 2 - WATTS Specification Sheet Capacity Series 757DCDA, 757NDCDA flow curves as tested by Underwriters Laboratory. Flow characteristics collected using butterfly shutoff valves Horizontal _____ Vertical ------N - Pattern • 21h" (65mm) PSI service Row Rated Flow lii. Rated Flow 14 - - - - - - J ifr1i1] t O 50 100 150 200 250 300 350 gpm 0 190 380 570 760 950 1140 1330 1pm 7.5 15 fps Flow capacity chart identifies valve performance based upon rated water velocity up to 25fps Service Flow is typically determined by a rated velocity of 7.5fps based upon schedule 40 pipe. Rated Flow identifies maximum continuous duty performance determined by AWWA. UL Flow Rate is 150% of Rated Flow and is not recommended for continuous duty. AWWA Manual M22 [Appendix Cl recommends that the maximum water velocity in services be not more than 10fps. 6" (150mm) I psi service Flow Rated Flow UL Rated Flow 12 -- N 10 ______ ______ ____ -. H ___ ___ __ i 6 00 8 - 4 1E__ 0 0 300 600 900 1200 1500 gpm I 0 1140 2280 3420 4560 5700 1pm 7.5 12 fps I I I I psi 12 10 6 U 0 0 0 psi 12 10 6 4 0 (80mm) psi Service Flow Rated Flow IJL Rated Flow 12 10 — 6 ow 0 0 100 200 300 400 500 0 380 760 1140 1520 1900 7.5 15 (100mm) Service Flaw Rated Row IJL Rated Flaw - - •1 - - - - .. 100 200 300 400 500 600 700 800 gpm 380 760 1140 1520 1900 2280 2660 3040 1pm 7.5 13 fps 8" (200mm) IlU;fl1I;f I U p I_ I I I I 500 1000 1500 2000 2500 gp 1900 3800 5700 7600 9500 Ip 7.5 10 fp I 10" (250mm) Service Flow Rated Row *UL Rated Flow JJIP 0 500 1000 1500 2000 2500 3000 3500 gp 0 1900 3800 5700 7600 9500 11400 13300 Ip 7.5 10 fps Ifti psi 24 20 16 12 cc z 00 8 0 0 0 N V H N N H V Inquire with governing authorities for local installation requirements !Th1 lil l[I It is illegal to use this product in any plumbing system providing water for human consumption, such as drinking or dishwashing, in the United States. Before installing standard material product, consult your local water authority, building and plumbing codes. I I I Attachment 2 - WATTS Specification Sheet I I U I I I I I I I I I I U I I i %%I WAT M A Watts Water Technologies Company USA: Tel: (978) 689-6066 • Fax: (978) 975-8350 • Wattscom Canada: Tel: (905) 332-4090 • Fax: (905) 332-7068 • Watts.ca Latin America: Tel: (52) 81-1001-8600 • Fax: (52) 81-8000-7091 • Watts.com ES-757DCDA_757NDCDA 1503 © 2015 Watts I I I I I I I I I I I I I I I I I I I 1 CARLSBAD ARE DEPARTMENT Fire Prevention Division 1635 Faraday Avenue - Carlsbad, CA 92008 760.602.4665 WATER AVAILABILITY FORM SECTION A: TO BE COMPLETED BY CUSTOMER PROJECT NAME: Shea Industrial SR#: (Assigned upon plan submittal) PROJECT ADDRESS: 6131& 6133 Innovation Way CITY: Carlsbad PHONE:( 619 ) 266-6030x103 FAX NUMBER: ( 619 ) 266-6035 Largest Building (ft.2): 54,775sf Sprinkled? YES Construction Type: Ill-B W/AS SECTION B: TO BE COMPLETED BY LOCAL WATER COMPANY. CUSTOMER TO PROVIDE RESULTS TO CFD. Water Purveyor: City of Carlsbad Location of test (reference map required): Innovation Way at Slater Drive TFST INFORMATION IS VALID WR 6 MONTHS FROM DATE PERFORMED Flow Test Results Static pressure: 74 PSI Hydrant Number (if applicable): H20918 Elevation of test: 379 Feet Date/rime of Test': Pitot Tube Reading: PSI Corresponding Flow: GPM Total Flow: 7.450 GPM Residual Pressure 38 PSI At peak demand, this water system is capable of providing a fire flow discharge @ 20 psi of no more than 9,450 GPM, but exceeds 15 fps. The maximum fire flow available at 15 fps is 7,450 GPM. Test to be performed as close as possible to the time the most conservative flows and pressures are expected. Note: If the water availability information was obtained in a manner other than a flow test (i.e. computer modeling), fill Out the information above as applicable and check here: . I have witnessed and/or reviewed this water flow information and by personal knowledge and/or on-site observation certify that the above information is correct. Name: Jennifer R. Mael, P.E. Eng. Lic. No. (if applicable):C69606 Signature: Title/Org: Date: 09/24/2015 50 0. 80 70 60 20 10 0 0 6131 & 6133 Innovation Way — Fire Sprinkler Curve iEE2EF _I U Allowable Fire Flow = 7,450 gpm H8a5e Maximum 5 fps d1 ma_ I ----_- ___ .' ----H--- -t --- ----t.- 1-••---- I —: - -._I - - . - Minimum 20 psi System Residual .- — -- -- H— — — - 4 -- ... - ---4 .- 1___ . .• ------r-----i-•-i----- _j Pressure . Flow exceeds Criteria -- -----..-----------t-------4--t-----:-----r H—_ . . J 1000 2000 3000 4000 5000 6000 7000 8000 9000 10000 Available Flow (gpm) 6131 & 6133 Innovation Way - Fire Flow Analysis JUrK.Ttcl TE') Acuve TK ROOTPE bA6waTut oiriii Tnk Adtie Reserior - omjn Reservoir go PIPE ihCT'PE) o ell / Pine %-Be P' ConiLci Pie 8 8" .--( /AceCheckVcie -. -•8 - - / - Domn Crek VIve • \d . FUhiP WOPiFf Active 9 . - muii SLATER PL H20918 U z? Domain I hvdrerls I a i fer. Ro 1 8" 8 • - 12" GATEWAY RD 12" 1 12' DIAM 'ALLEY U Prepared By: Jennifer R. Masi, PE - MCS Date: Thursday, September 24, 2015 I I I I I I I I I I I I I I I I I I I Attachment 4 Network Table - Links Link ID Length ft Diameter in Flow GPM Velocity fps Pump 19 #N/A #N/A 1750.00 0.00 Pipe 17 26.69 6 0.00 0.00 Pipe 18 24.87 6 0.00 0.00 Pipe 16 14.74 6 0.00 0.00 Pipe 15 13.46 6 0.00 0.00 Pipe 7 23.38 8 0.00 0.00 Pipe 8 26.04 8 0.00 0.00 Pipe 13 5 6 0.00 0.00 Pipe 12 11.86 6 0.00 0.00 Pipe 25 66.59 6 0.00 0.00 Pipe 11 28.75 6 0.00 0.00 Pipe 14 30.79 6 0.00 0.00 Pipe 21 55 12 1750.00 4.96 Pipe 20 84.4 12 1750.00 4.96 Pipe 9 107.22 8, 1000.00 6.38 Pipe 6 218.87 8 1000.00 6.38 Pipe 3 26.32 10 1750.00 7.15 Pipe 4 77.66 10 1750.00 7.15 Pipe 26 36 10 -1750.00 7.15 Pipe 27 13.01 10 -1750.00 7.15 Pipe 23 1 10 1750.00 7.15 Pipe 5 24 6 750.00 8.51 Valve 22 #N/A 8 1750.00 11.17 Pipe 10 21 6 1000.00 11.35 Page 1 Attachment 5 Network Table - Nodes Node ID Elevation ft Demand GPM Head ft Pressure psi Resvr28 379 -1750.00 379.00 0.00 Junc 11 374.09 0.00 507.37 57.75 June 6 372.73 1000.00 506.18 57.82 Junc 10 373.29 0.00 507.37 58.10 Junc9 373.16 0.00 507.37 58.15 Junc 8 372.85 0.00 507.37 58.29 Junc 7 372.73 0.00 507.37 58.34 Junc 29 378.52 0.00 513.98 58.69 Junc 23 378.35 0.00 513.99 58.77 June 15 376.8 0.00 513.81 59.36 June 5 371.44 0.00 508.87 59.55 Junc 24 373.17 750.00 511.14 59.78 June 4 370.6 0.00 508.87 59.91 June 12 373.01 0.00 511.94 60.20 June 19 374.15 0.00 513.33 60.31 June 3 369.55 0.00 508.87 60.37 June 14 373.87 0.00 513.33 60.43 Junc 22 373.7 0.00 513.33 60.50 Junc 21 373.7 0.00 513.33 60.50 Junc 20 373.7 0.00 513.33 60.50 June 13 373.21 0.00 512.98 60.56 June 1 368.07 0.00 508.87 61.01 June 25 378.35 0.00 528.99 65.27 June 26 378.35 0.00 529.29 65.40 June 27 376.6 0.00 529.75 66.36 Pagel 1 I I I I I I I I I I I I I I I I Li I I I I I I I I I I I I I I I I I I I I Attachment 6 Network Table - Links Link ID Length ft Diameter in Flow GPM Velocity fps Pump 19 #N/A #N/A 2000.00 0.00 Pipe 7 23.38 8 0.00 0.00 Pipe 8 26.04 8 0.00 0.00 Pipe 15 13.46 6 0.00 0.00 Pipe 18 24.87 6 0.00 0.00 Pipe 16 14.74 6 0.00 0.00 Pipe 17 26.69 6 0.00 0.00 Pipe 25 66.59 6 0.00 0.00 Pipe 14 30.79 6 250.00 2.84 Pipe 11 28.75 6 250.00 2.84 Pipe 12 11.86 6 250.00 2.84 Pipe 13 5 6 250.00 2.84 Pipe 20 84.4 12 2000.00 5.67 Pipe 21 55 12 2000.00 5.67 Pipe 9 107.22 8 1250.00 7.98 Pipe 6 218.87 8 1250.00 7.98 Pipe 4 77.66 10 2000.00 8.17 Pipe 3 26.32 10 2000.00 8.17 Pipe 27 13.01 10 -2000.00 8.17 Pipe 23 1 10 2000.00 8.17 Pipe 26 36 10 -2000.00 8.17 Pipe 5 24 6 750.00 8.51 Pipe 10 21 6 1000.00 11.35 Valve 22 #NIA 8 2000.00 12.77 Page 1 Attachment 7 Network Table - Nodes Node ID Elevation ft Demand GPM Head ft Pressure psi Resvr 28 379 -2000.00 379.00 0.00 Junc 11 374.09 250.00 497.67 53.55 June 6 372.73 1000.00 496.81 53.76 June 10 373.29 0.00 497.81 53.95 June 9 373.16 0.00 497.83 54.02 Junc8 372.85 0.00 497.88 54.18 Junc 7 372.73 0.00 498.00 54.28 Junc5 371.44 0.00 500.28 55.82 Junc 29 378.52 0.00 507.52 55.90 Junc 23 378.35 0.00 507.54 55.98 June 4 370.6 0.00 500.28 56.19 Junc 15 376.8 0.00 507.30 56.55 June 3 369.55 0.00 500.28 56.64 Junc 24 373.17 750.00 504.11 56.74 June 12 373.01 0.00 504.91 57.15 June 1 368.07 0.00 500.28 57.28 June 19 374.15 0.00 506.69 57.43 June 14 373.87 0.00 506.69 57.55 Junc 22 373.7 0.00 506.69 57.62 Junc 21 373.7 0.00 506.69 57.62 June 20 373.7 0.00 506.69 57.62 June 13 373.21 0.00 506.24 57.64 June 25 378.35 0.00 525.99 63.97 Junc 26 378.35 0.00 526.38 64.14 June 27 376.6 0.00 526.97 65.16 Pagel 1 El I I I I I Li I I I I I I I I I