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Specifications 729B' S u✓ !ec.I.GYche-c D r 6002.064 OO1 (ocl Bulletin 129 Rev co c •■ Model G XLO Extra Large Orifice Sprinkler h Extra Large Orifice Sprinkler (SIN 82921) Features t i . '' The Reliable Model G XLO sprinkler offers they opportunity for: 1. Pipe size reduction ¢i '' -• `� 2. Fewer sprinklers tr . 3. Elimination of booster pumps -~ 4. Increasing densities with existing systems 5. Y NPT (R available for retrofit installations only. This product is intended for use as a standard spray sprinkler in hydraulically designed systems 6. Also includes additional Specific Application listing. with a minimum pressure of 7 psi (0.5 bar) in accor- (See detailed "UL on Application listing" dance with the area/density curves of NFPA 13* stan- described on the back page.) dards and for all area/density methods of design as Listin S & A royals' referenced by Factory Mutual (FM) Prevention Data 1. Listed by Underwriters Laboratories, Inc. (UL) Sheets. 2. Listed by Underwriters Laboratories' of Canada (ULC) Design Criteria 3. Approved by Factory Mutual (FM) The following criteria apply when designing an automatic sprin- 4. NYC MEA 258-93 -E (NFPA 131. kler system tang the Model G XLO sprinkler for NFPA 13* appli UL Guide Number - .. cations. VNIV Sprinkler spacing shall be a minimum of 6 ft. (1.8m) with Y UL Listing Category Sprinklers wi NPT (Rh) are to be used for retrofit 9 eg ry applications only. Sprinklers, Automatic & Open Extra Large Orifice Sprinkler discharge pressure per NFPA 13* standards I Upright Sprinkler and Specific Application Sprinkler. shall be a minimum of 7 psi (0,5 bar). Technical Data � discharge pressure for NFPA 13* standard and K Favor all Factory Mutual (FM) applications shall be a minirrurn of Nominal 10 psi (0.7 bar). US fdleblc Ser Approvals N Factory Mutual (FM) Loss Prevention Data Sheets contain Upright • requirements which differ from NFPA. The Model G XLO 0.64 Orifice with 11.2 160 3.14 1,2,3,4 R2921 is Approved by Factory Mutual for all area/density 3 4 NPT (RIO (80mm) methods of design as referenced by FM Loss Prevention Upright Retrofit 0.64Orfice with 11.2 160 (83mm) Data 1,2,3,4 R2921 Sheets. 1 / NPT (ref`) The Model G XLO Extra Large Orifice sprinkler is intended for Note: This product has been tested and listed for storage appli- standard flow/pressure requirements and standard place- cations to qualify its use in lieu of 5.6K or 8.0K Factor sprinklers ment as specified for NFPA storage requirements. The Model for the protection of high - piled storage. G XLO sprinkler is not a "Large Drop" or'ESFR" sprinkler. Product Description The Reliable Model G XLO sprinkler is a center strut Temperature Ratings solder in compression extra large orifice upright sprinkler that has been designed to control high chal- Ma:dinun Ambient lenge fires in both palletized and rack storage occu- Orr Frame Cal or pancies utilizing relatively low water pressures. This sprinkler is available with either the standard'. NPT Ordinary 165 74 100 38 Uncolored (R 3 /a) threads for new installations or with X NPT (RY) Intermediate 212 100 150 66 White threads for retrofit applications. High 286 141 225 107 Blue It has been proven in full -scale fire testing, has com- plied with the applicable mechanical and hydraulic sections of the latest sprinkler standards and has Fac- • For sprinkler standards prior to 1999 edition of NFPA 13, tory Mutual Approval and Underwriters Laboratories use NFPA standards 231, 231C, 231D & 231F. and Underwriters Laboratories' of Canada Listings. The Reliable Automatic SprinlderCo Inc. • 525 North MacQuesh3n Parkway • Mount Vernon • New York • 10552 ., • Finishes Maintenance Standard Finishes Model G XLO Sprinklers should be inspected quarterly and n the sprinkler system maintained in accordance with NFPA Bronze Chrome 25. Do not clean sprinklers with soap and water, ammonia or Special Application Finishes or other cleaning fluids. Remove dust by using a soft brush or gentle vacuuming. Remove sprinkler which has been Lead Plated"' -165 F (74 C), 212 F (100 C) and painted (other than factory applied) or damaged in any way. 286 F (141 C) Temp. Ratings A stock of spare sprinklers should be maintained to allow l (100 C) B Wax MO - 165 F (74 C) Clan Wax 212 F (dick replacement of of 10) rown ax W � operated sprinklers. Prior Wax/Lead t° ( F C) Clear wax to installation, sprinklers should be maintained in the original 2 F (100 C) Brown wax cartons and pa-cka.agin.g until used to minimize the potential (1) UL Listed only. for or t�9 � ens that would cause improper opera - (2) 212 F (100 C) Brown wax may be used on 286 F (141 C) Sprinklcrs when maximum ambient temperatures do not exceed 150 F (66 C). Ordering Information The UL Specific Application Listing is: 1. Sprinkler Model The Model G XLO upright sprinkler is intended for use in 2. Temperature Rating I accordance with NFPA 13* standards when installed in 3. Finishes accordance with the standard sprinkler positioning and area/density flow calculation requirements as specified in I each respective standard. Model G XLO upright sprinklers may also be installed to protect single, double and multiple - Model H Sprinkler Wrench row and portable rack sludge of Class I-IV, Groups A and B Use only the Model H plastics, =toned, expanded or unexpended, as well as sprinkler wrench for exposed unexpended with a maximum storage height of 20 ft. ' X . : ki _� , i �nstalMation other (6.5m), maxdmum calling height of 25 ft. (8.2m)) or 27" ft (8.8m) - -- maximum ceiling height, 36 (914mm) minimum deflector to " ° • type of wrench may damage the sprinkler. top of storage clearance, design density of 0.60 g ft (24.7 Umirym and a design area of 20X)0 fi (186mm') for wet systems and 2600 ft (242m for dry systems. "Note: Maximum ceilling height is allowed by NFPA 13", without in-rack sprinklers in a protected area, provided the ceiling sprinklers' discharge is increased to 0.6 gprrtill in a ' 2000 ft design area r a • 1i Installation Reliable's Model G XLO sprinkler must be installed (r,'r NM 2.82 , 3.25 (r /2• not) I according to NFPA Standards or the appropriate In.6mml - ''� !x•61 Factory Mutual Loss Prevention Data Sheets for all (.1/4" NPn 2.71 : 1 s r, rs/o WI) area/density methods of design as well as the l wksoo I Authority Having Jurisdiction. >•__IMMI. The Model GXLO sprinkler meets the NFPA 13" c star- - pp roval & Fact ory M utual and lis t i ngs Under - —r writers Laboratories Underwriters Underwriters laboratories of Canada r,er -1— (47.5awal * For sprinkler standards prior to 1999 edition of NFPA 13, use NFPA standards 231, 231C, 231D & 231F. The equipment presented in this bulletin is to be installed In accordance with the latest pertinent Standards of the National Fire Protection Association, Factory Mutual Research Corporation, or other similar organizations and also with the provisions of governmental codes or ordinances whenever applicable. Products manufactured and distributed by Reliable have been protecting life and property for over 80 years, and are installed and serviced by the most highly qualified and reputable sprinkler contractors located throughout the United States, Canada and foreign countries. Manufactured by ple lit The Reliable Automatic Sprinkler co., Inc. ( 600 ) 431 - Sales Offi ces (800) 848-6051 Sales Fax Revision lines indicate updated or new data (914) 668 Corporate Offices PG Printed m U SA 06102 PM9999970022 www retiablesprmlder corn Internet Address PARKER FIRE PROTECTION, INC. p 2 0.04 Lf _ © p'4 -(p 9' 30205 SE KELSO ROAD BORING,OR 97009 HYDRAULIC CALCULATIONS FOR Multi -Craft Plastics FILE NUMBER: DATE: SEP 28, 2004 - DESIGN DATA - OCCUPANCY CLASSIFICATION: Class IV Commodity DENSITY: .31 gpm /sq. ft. AREA OF APPLICATION: 3000 sq. ft. COVERAGE PER SPRINKLER: 120 sq. ft. NUMBER OF SPRINKLERS CALCULATED: 25 sprinklers TOTAL SPRINKLER WATER FLOW REQUIRED: 994.4 gpm TOTAL WATER REQUIRED (including hose): 1244.4 gpm FLOW AND PRESSURE (8 BOR): 994.4 gpm 8 66.0 psi SPRINKLER ORIFICE SIZE: 1/2 inch NAME OF CONTRACTOR: Parker Fire Protection, Inc. DESIGN /LAYOUT BY: Colby Statchwick AUTHORITY HAVING JURISDICTION: City of Tigard CONTRACTOR CERTIFICATION NUMBER: 124300 CALCULATIONS BY HASS COMPUTER PROGRAM (LICENSE # 27100958 ) HRS SYSTEMS, INC. TUCKER, GA 30084 ' SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 2 DATE: 9/28/2004 C: \HASS76 \MULTI CRAFT PLASTICS.SDF JOB TITLE: Multi -Craft Plastics ' WATER SUPPLY DATA SOURCE STATIC RESID. FLOW AVAIL. TOTAL REQ'D NODE PRESS. PRESS. @ PRESS. @ DEMAND PRESS. TAG (PSI) (PSI) (GPM) (PSI) (GPM) (PSI) SOURCE 92.0 82.0 1500.0 84.9 1244.4 70.1 AGGREGATE FLOW ANALYSIS: TOTAL FLOW AT SOURCE 1244.4 GPM TOTAL HOSE STREAM ALLOWANCE AT SOURCE 250.0 GPM OTHER HOSE STREAM ALLOWANCES 0.0 GPM TOTAL DISCHARGE FROM ACTIVE SPRINKLERS 994.4 GPM NODE ANALYSIS DATA PRESSURE NODE TAG ELEVATION NODE TYPE TOTAL NORMAL DISCHARGE (FT) (PSI) (PSI) (GPM) S1 25.0 K =11.20 11.5 11.5 38.0 S2 25.0 K =11.20 12.1 11.1 37.3 S3 25.0 K =11.20 13.9 11.8 38.4 S4 25.0 K =11.20 18.0 13.9 41.8 S5 25.0 K =11.20 18.0 13.9 41.8 S6 25.0 K =11.20 13.9 11.8 38.4 S7 25.0 K =11.20 12.1 11.1 37.3 S8 25.0 K =11.20 11.5 11.5 38.0 S9 25.0 K =11.20 11.4 11.4 37.9 S10 25.0 K =11.20 12.0 11.0 37.2 Sil 25.0 K =11.20 13.8 11.7 38.3 S12 25.0 K =11.20 17.8 13.8 41.6 S13 25.0 K =11.20 17.8 13.8 41.6 S14 25.0 K =11.20 13.8 11.7 38.3 S15 25.0 K =11.20 12.0 11.0 37.2 S16 25.0 K =11.20 11.4 11.4 37.9 S17 25.0 K =11.20 11.5 11.5 37.9 S18 25.0 K =11.20 12.0 11.0 37.2 S19 25.0 K =11.20 13.8 11.7 38.3 S20 25.0 K =11.20 17.9 13.8 41.7 S21 25.0 K =11.20 17.9 13.8 41.7 S22 25.0 K =11.20 13.8 11.7 38.3 S23 25.0 K =11.20 12.0 11.0 37.2 S24 25.0 K =11.20 11.5 11.5 37.9 S25 25.0 K =11.20 31.5 31.5 62.9 M1 24.0 - - - - 33.3 32.0 - - - M1A 25.0 - - - - 24.4 18.5 - - - M2 24.0 - - - - 33.1 32.8 - - - M2A 25.0 - - - - 24.3 18.4 - - - M3 24.0 - - - - 33.1 32.5 - - - M3A 25.0 - - - - 24.3 18.4 - - - M4 24.0 - - - - 33.6 32.8 - - - ' SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 3 DATE: 9/28/2004 C: \HASS76 \MULTI CRAFT PLASTICS.SDF JOB TITLE: Multi -Craft Plastics NODE ANALYSIS DATA PRESSURE NODE TAG ELEVATION NODE TYPE TOTAL NORMAL DISCHARGE (FT) (PSI) (PSI) (GPM) M4A 25.0 - - - - 32.7 32.5 - - - M5 24.0 - - - - 49.0 48.1 - - - TOR 24.0 - - - - 51.9 51.1 - - - BOR -3.0 - - - - 66.0 66.0 - - - DSD -3.0 - - - - 66.7 66.7 - - - . SSD -3.0 - - - - 69.7 69.7 - - - SOURCE -3.0 SOURCE 70.1 70.1 994.4 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 4 DATE: 9/28/2004 C: \HASS76 \MULTI CRAFT PLASTICS.SDF JOB TITLE: Multi -Craft Plastics ' PIPE DATA PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. PT PN DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (PSI) (PSI) (GPM) FL /FT (PSI) Pipe: 1 -38.0 1.610 PL 10.00 PF 0.5 S1 25.0 11.5 11.5 38.0 6.0 120 FTG - - -- PE 0.0 S2 25.0 12.1 11.1 37.3 0.053 TL 10.00 PV 0.2 Pipe: 2 -75.4 1.610 PL 10.00 PF 1.9 S2 25.0 12.1 11.1 37.3 11.9 120 FTG - - -- PE 0.0 S3 25.0 13.9 11.8 38.4 0.188 TL 10.00 PV 0.9 Pipe: 3 -113.8 1.610 PL 10.00 PF 4.0 S3 25.0 13.9 11.8 38.4 17.9 120 FTG - - -- PE 0.0 S4 25.0 18.0 13.9 41.8 0.403 TL 10.00 PV 2.2 Pipe: 4 -155.6 1.610 PL 5.00 PF 6.5 S4 25.0 18.0 13.9 41.8 24.5 120 FTG E PE 0.0 M1A 25.0 24.4 18.5 0.0 0.719 TL 9.00 PV 4.0 Pipe: 5 155.6 1.610 PL 5.00 PF 6.5 M1A 25.0 24.4 18.5 0.0 24.5 120 FTG E PE 0.0 S5 25.0 18.0 13.9 41.8 0.719 TL 9.00 PV 4.0 Pipe: 6 113.8 1.610 PL 10.00 PF 4.0 S5 25.0 18.0 13.9 41.8 17.9 120 FTG - - -- PE 0.0 S6 25.0 13.9 11.8 38.4 0.403 TL 10.00 PV 2.2 Pipe: 7 75.4 1.610 PL 10.00 PF 1.9 S6 25.0 13.9 11.8 38.4 11.9 120 FTG - - -- PE 0.0 S7 25.0 12.1 11.1 37.3 0.188 TL 10.00 PV 0.9 Pipe: 8 38.0 1.610 PL 10.00 PF 0.5 S7 25.0 12.1 11.1 37.3 6.0 120 FTG - - -- PE 0.0 S8 25.0 11.5 11.5 38.0 0.053 TL 10.00 PV 0.2 Pipe: 9 -37.9 1.610 PL 10.00 PF 0.5 S9 25.0 11.4 11.4 37.9 6.0 120 FTG - - -- PE 0.0 S10 25.0 12.0 11.0 37.2 0.053 TL 10.00 PV 0.2 Pipe: 10 -75.1 1.610 PL 10.00 PF 1.9 S10 25.0 12.0 11.0 37.2 11.8 120 FTG - - -- PE 0.0 Sll 25.0 13.8 11.7 38.3 0.187 TL 10.00 PV 0.9 Pipe: 11 -113.4 1.610 PL 10.00 PF 4.0 ' S11 25.0 13.8 11.7 38.3 17.9 120 FTG - - -- PE 0.0 S12 25.0 17.8 13.8 41.6 0.400 TL 10.00 PV 2.1 Pipe: 12 -155.0 1.610 PL 5.00 PF 6.4 S12 25.0 17.8 13.8 41.6 24.4 120 FTG E PE 0.0 M2A 25.0 24.3 18.4 0.0 0.714 TL 9.00 PV 4.0 SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 5 DATE: 9/28/2004 C: \HASS76 \MULTI CRAFT PLASTICS.SDF JOB TITLE: Multi -Craft Plastics PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. PT PN DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (PSI) (PSI) (GPM) FL /FT (PSI) Pipe: 13 155.0 1.610 PL 5.00 PF 6.4 M2A 25.0 24.3 18.4 0.0 24.4 120 FTG E PE 0.0 an 25.0 17.8 13.8 41.6 0.714 TL 9.00 PV 4.0 Pipe: 14 113.4 1.610 PL 10.00 PF 4.0 S13 25.0 17.8 13.8 41.6 17.9 120 FTG - - -- PE 0.0 S14 25.0 13.8 11.7 38.3 0.400 TL 10.00 PV 2.1 Pipe: 15 75.1 1.610 PL 10.00 PF 1.9 S14 25:0 13.8 11.7 38.3 11.8 120 FTG - - -- PE 0.0 S15 25.0 12.0 11.0 37.2 0.187 TL 10.00 PV 0.9 Pipe: 16 37.9 1.610 PL 10.00 PF 0.5 S15 25.0 12.0 11.0 37.2 6.0 120 FTG - - -- PE 0.0 S16 25.0 11.4 11.4 37.9 0.053 TL 10.00 PV 0.2 Pipe: 17 -37.9 1.610 PL 10.00 PF 0.5 S17 25.0 11.5 11.5 37.9 6.0 120 FTG - - -- PE 0.0 S18 25.0 12.0 11.0 37.2 0.053 TL 10.00 PV 0.2 Pipe: 18 -75.1 1.610 PL 10.00 PF 1.9 S18 25.0 12.0 11.0 37.2 11.8 120 FTG - - -- PE 0.0 S19 25.0 13.8 11.7 38.3 0.187 TL 10.00 PV 0.9 Pipe: 19 -113.4 1.610 PL 10.00 PF 4.0 S19 25.0 13.8 . 11.7 38.3 17.9 120.FTG - - -- PE 0.0 S20 25.0 17.9 13.8' 41.7 - 0.400 TL 10.00 PV 2.1 Pipe: 20. - 155.1 1.610 PL 5.00 PF .6.4 ' S20 .25.0 17.9 13.8 . 41.7 24.4. . 120 FTG E PE 0.0 M3A 25.0 24.3 , 18.4 0.0 0.714.TL 9.00 PV 4.0 Pipe: 21 155.1 1.610 PL 5.00 PF 6.4 M3A 25.0 24.3 18.4 0.0 24.4 120 FTG E PE 0.0 S21 25.0 17.9 13.8 41.7 0.714 TL 9.00 PV 4.0 Pipe: 22 113.4 1.610 PL 10.00 PF 4.0 S21 25.0 17.9 13.8 41.7 17.9 120 FTG - - -- PE 0.0 S22 25.0 13.8 11.7 38.3 0.400 TL 10.00 PV 2.1 Pipe: 23 75.1 1.610 PL 10.00 PF 1.9 S22 25.0 13.8 11.7 38.3 11.8 120 FTG - - -- PE 0.0 S23 25.0 12.0 11.0 37.2 0.187 TL 10.00 PV 0.9 Pipe: 24 37.9 1.610 PL 10.00 PF 0.5 S23 25.0 12.0 11.0 37.2 6.0 120 FTG . - - -- PE 0.0 S24 25.0 11.5 11.5 37.9 0.053 TL 10.00 PV 0.2 Pipe: 25 -62.9 1.610.PL 5.00 PF 1.2 S25 25.0 31.5 31.5 62.9 9.9 120 FTG E PE 0.0 M4A 25.0 32.7 32.5 0.0 0.134 TL 9.00 PV 0.7 • SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 6 DATE: 9/28/2004 C: \HASS76 \MULTI CRAFT PLASTICS.SDF JOB TITLE: Multi -Craft Plastics PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. PT PN DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (PSI) (PSI) (GPM) FL /FT (PSI) Pipe: 26 -311.3 2.067 PL 1.00 PF 8.4 M1A 25.0 24.4 18.5 0.0 29.8 120 FTG T PE 0.4 M1 24.0 33.3 32.0 0.0 0.768 TL 11.00 PV 6:0 Pipe: 27 -310.1 2.067 PL 1.00 PF 8.4 M2A 25.0 24.3 18.4 0.0 29.6 120 FTG T PE 0.4 •M2 24.0 33.1 32.8 0.0 0.762 TL 11.00 PV 5.9 Pipe: 28 -310.2 2.067 PL 1.00 PF 8.4 M3A 25.0 24.3 18.4 0.0 29.7 120 FTG T PE 0.4 M3 24.0 33.1 32.5 0.0 0.763 TL 11.00 PV 5.9 Pipe: 29 -62.9 2.067 PL 1.00 PF 0.4 M4A 25.0 32.7 32.5 • 0.0 6.0 120 FTG T PE 0.4 M4 24.0 33.6 32.8 0.0 0.040 TL 11.00 PV 0.2 Pipe: 30 249.1 4.026 PL 12.00 PF 0.2 M1 24.0 33.3 32.0 0.0 6.3 120 FTG - - -- PE 0.0 M2 24.0 33.1 32.8 0.0 0.020 TL 12.00 PV 0.3 Pipe: 31 -61.0 4.026 PL 11.17 PF 0.0 M2 24.0 33.1 32.8 0.0 1.5 120 FTG - - -- PE 0.0 M3 24.0 33.1 32.5 0.0 0.001 TL 11.17 PV 0.0 Pipe: 32 -371.1 4.026 PL 12.00 PF 0.5 M3 24.0. 33.1 32,.5 •. 0.0 9.4 120 FTG - - -- . PE 0.0 M4 24.0 ._33.6 32.8 - 0.0 - • 0.041 TL 12.00 PV • 0.6 Pipe : 33 - 434. 4 :026 -PL 247.92 PF . 15.4 • , M4 • .2 33.6 . 32.8 .0.0 10.9 120 FTG . 3E PE 0.0 • M5 '24.0 •49.0 48.1 , 0.0 0.055 TL '277.92 PV 0.8 . Pipe: 34 -560.4 4.026 PL 146.33 PF 15.6 M1 24.0 33.3 32.0 0.0 14.1 120 FTG 3E PE 0.0 M5 24.0 49.0 48.1 0.0 0.089 TL 176.33 PV 1.3 Pipe: 35 -994.4 6.065 PL 58.00' PF 3.0 M5 24.0 49.0 48.1 0.0 11.0 120 FTG 2E PE 0.0 TOR 24.0 51.9 51.1 0.0 0.035 TL 86.00 PV 0.8 Pipe: 36 -994.4 6.065 PL 27.00 PF 2.4 TOR 24.0 51.9 51.1 0.0 11.0 120 FTG EA PE 11.7 BOR -3.0 66.0 66.0 0.0 0.035 TL 69.00 PV 0.8 Pipe: 37 -994.4 10.400 PL 265.00 PF 0.7 BOR -3.0 66.0 66.0 0.0 3.8 140 FTG 3E PE 0.0 DSD -3.0 66.7 66.7 0.0 0.002 TL 370.00 PV 0.1 Pipe: 38 FIXED PRESSURE LOSS DEVICE SSD -3.0 0.0 69.7 0.0 3.0 psi, 994.4 gpm DSD -3.0 0.0 66.7 0.0 • SPRINKLER SYSTEM HYDRAULIC' ANALYSIS Page 7 DATE: 9/28/2004 C: \HASS76 \MULTI CRAFT PLASTICS.SDF JOB TITLE: Multi -Craft Plastics • PIPE TAG Q(GPM) DIA(IN) LENGTH PRESS. END ELEV. PT PN DISC. VEL(FPS) HW(C) (FT) SUM. NODES (FT) (PSI) (PSI) (GPM) FL /FT (PSI) Pipe: 39 -994.4 8.390 PL 10.00 PF 0.4 SSD -3.0 69.7 69.7 0.0 5.8 140 FTG T PE 0.0 SOURCE -3.0 70.1 70.1 (N /A) 0.005 TL 69.00 PV 0.2 NOTES: V • (1) Calculations were performed by the HASS 7.6 computer program under license no. 27100958 granted by HRS Systems, Inc. 4792 LaVista Road Tucker, GA 30084 (2) The .system has been calculated to provide an average imbalance at each node of 0.003 gpm and a maximum imbalance at any node of 0.099 gpm. V (3) Velocity pressures have been included in the calculation of the system pressures and flows. Maximum water velocity is 29.8 ft /sec at pipe 26. (4) PIPE FITTINGS TABLE . Pipe Table Name: STANDARD.PIP • PAGE: A MATERIAL:, 040 HWC: 12 • • Diameter '' Equivalent Fitting Lengths in Feet (in) E T. L, . 'C Ell Tee 'LngEll•ChkVly BfyVly GatVly AlmChk DPVly NPTee 1.610 4.00 8.00 2 . 9.00 ' 6.00 1.00 10.00 10.00 8.00 • V 2.067 5.00 10.00 3.00 11.00 6.00 1.00 10.00 10.00 10 :00 4.026 10.00 20.00 6.00 22.00 12.00 2.00 20.00 20.00 20.00 6.065 14.00 30.00 9.00 32.00 10.00 3.00 28.00 28.00 30.00 PAGE: D MATERIAL: DIRON HWC: 140 Diameter Equivalent Fitting Lengths in Feet (in) E T L C B G N Ell Tee LngEll ChkVly BfyVly GatVly NPTee 8.390 31.00 59.00 22.00 76.00 20.00 7.00 59.00 10.400 35.00 80.00 26.00 88.00 30.00 8.00 80.00 • ct7 C WATER SUPPLY ANALYSIS -3 " 100.0 Static: 92.00 psi Resid: 82.00 psi Flow: 1500.0 gpm H W LEGEND r Cr) N - op Available pressure J. 84.92 psi @ 1244.4 gpm 0 o R pressure F'' CD 1 2 a 70.12 psi @ 1244.4 gpm r A. Source Supply Curve 0 G 80.0 _ m B System Demand Curve K A w n cn U ct ro G 2 PO H E w x CA t cr to P 60.0 _ o ti R K E co H S to S U x K E 40.0 _ d C] x iC xr ,b H ( (n C) N p -4 > rn z S > i 0 K ) 20.0 _ H H H U) C) H rd 0.0 B �, cn H H O ro W w • w v) m -14.7 I I I I I I I I 1 o0 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM) ' SPRINKLER SYSTEM HYDRAULIC ANALYSIS Page 9 DATE: 9/28/2004 C: \HASS76 \MULTI CRAFT PLASTICS.SDF JOB TITLE: Multi -Craft Plastics ' WATER SUPPLY CURVE 96+ . I * \ \ \ \ \ \\ I \ \ \ \ \ \ \\ 88+ \ \ \ \ \ \\ I \ \ \ \ \ \ \\ I 0 \ \ \ \ \ \\ I * < -82.0 psi @ 1500 gpm 80+ Flow Test Point I I I 72+ I x 1 I P 64+ R I E I S I S 56+ U I R I E I 48+ ( I P S I I 40+ ) I I I 32+ I I 1 24+ I I I 16+ LEGEND " I " I X = Required Water Supply " I 70.12 psi @ 1244.4 gpm " 8+ If 1 0 = Available Water Supply " I 84.92 psi @ 1244.4 gpm " I " 0 + +- +--- +- -- -+ + + + + + + 400 600 800 1000 1200 1400 1600 1800 2000 FLOW (GPM)