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HomeMy WebLinkAbout50 Talbot Lane - Building Plans & Drawin Remote Area 2 Flawing Heads 9 Start Head PSI 20.7 Remote Area 1 Ravine Heads 9 IS IM Head PSI 24.0 Ill/Dry NET Density 0.200 Start Head GPM 51.0 Net/Ory WET Density 0.200 Slwt Head OF SILO Hazard ORDINARY 2 Ilueo I500 SOFT per Hand 255 Hazard ORDINARY 2 An. 1500 SOFT par Head 255 Code NFPA 13 Len/Mal Ratio 1.20 El.,Hd to Rlaar(') 318 Ced. NFPA 13 Len/Md Ratio 1.20 EIS,Hd to Riser 1')318 Construction Max Velocity 19.1 PSI -Hd to Riser 11.5 Conslmellon Max Velocity 9.30 PSI-Hd to Riser 11.5 Source Name or Location Sauna Source Name or Location Source - Remote Area 3 Flonin. Heads Ii Sta I Nead PSI 26.0 THIS CALCULATION 15 FOR PSI AwR at Source 70.1 GPM Req'd at Source 747 Inside Hose 0.000 PSI Awl at Source 78.5 GPM Req'd at Source 721 inslde Hose 0.000 THIS CALCULATION IS FOR Wal/Dry WET Dewily OLIO( Stall Nead GPM 30.0 PENDENT SPRINKLERS PSI Faq'd at Source 59.6 Duration of Source 0.000 lOutsida Hose 250 PSI^eq'd at Source 48.4 Ouration of Source GOOD jOulsida Hose 250 UPRIGHT SPRINKLERS Hazard LIGHT Are. 1500 SOFT par Head 225 Safely PSI 18.5 Req'd Source Volume 0.000 Safety PSI 30.0 Req'd Source Volume 0,0013 Coda NFPA 13 Len/Wid Ratio 1.20 Ba-Hd to Rise,er(')318 Awllable Pressure of 78.1 psi Exceeds Required Pressure a(59.6 Pal Pressure Available Preeevre of 78.5 psi Exceeds Required Pressure of 48.4 Psi Construction Max Velocity 21.4 PSI,-Hd to Riser 11.5 Summary j This Is a safely margin of 18.5 psi or 24 S of Supply Summary I This I9 a safety margin of 30.0 psi or 38%of Supply Source Name or Location Source Advanced IMo.0...Ity AwLloble 0.229 IPS lass- TOR to Saurce 4.40 Advanced IMax Density AwlaIde 0.255 IPS loss-TOR to Source 4.28 PSI Awl at Source 82.4 ICPM Req'd at Source 363 1 (Inside Hasa 0.000 Summary GPM at Mo.Awl.ble Density 055 Rock Demand 0.000 Summary GPM at Mo.Awlabla Density 918 Rack Demand (LOGO PS Req'd at Source 53.6 Duratlan of Saurce 0.000) Oubide Hose 100 Safely PSI 28.0 Req'd Source Volume 0.(00, Spressureummary IAwllable Pressure er la o 28 psi or Required Pressure of 53.6 psi 3.5 4.5 5 5.5 7.5 8 9 9.3 9.7 10 11 [ Summary ThisAw is.solely margin of psi psi.r Re ui of Supply Adwnced I Max Density Available0.124 jPS Iosa - TOR to Source 4.04 Summary GPM at Max Awllable Density 450 flock Be and 0.000 I I I I I I N j j I SEE ETSAT - EXACT LOCATIO [ 0 CO OF ICE r 51 LL R001 R LE n O 0i A 0 26 - I-Z4 Of'-2 1 - -1 -- 120 -,-4-. - E2 - -- -I- - - - - 1 - -- -- m d j iJPTJ 4 2, 23 2 [ 33 - _ RLIT E3 C I 2 2 I• t t . i ", R001 s 72 I B 4 IW 11-0 II-0 IFO 1-0 I 1}0 IYB 1}0 10 I I I}0 I6 0 I6-0 I • 7- -u'o 1z4 _- -t23 ,2z 1 , E4 I A (AGING I ° PA FEANG O _ �- - 136_ _ - _ _ -- I - -. _-_ -__ _-_ 177- - -. - • - --- -- T"- -- a ' j-5)S 2 N 0 5PR1 KLEftS UNDER PLATF RM SEE HEET P PP006 S I r [ I 2 • 128 -- O • O - PI35 . 3 CS _ _-EN OFA'E n. � T �___uL_ O • - 11 A200 • ' I}B a • __ C FEppE E-� M-0 14-0 1" II-1 I I}l I e M-0 14-0 I f I 19 t6-0 IFO I}l 1 A203 1- ®OO'J O !_- m I 1! S IX1A , WOMEN'S 3 I OR • _ ROOM I • • Q _ - A210 t_ f • • • - --1 - =�l f-,� C• _ _ I I 1 li 6-] I II l I-91 -61, 5-/b • & I I^ 0 II-0 I� I4-0 II-0 - I 11-a I B II-a I I 9 I}0 I6-0 I6 O I -OFFICE- "C�_ Ir _JI ' _ _ _ _ I 'll- - • At mn rtrn m-n TRmr A214 _ A213 QIAEN'S 1 �- )' _ _ 0 RDDM >S� u� 1W 1 yl IJj ull �� I' 2 6-Mr ` 1' 119' • • A21-1 -1 _ •I v( j I.roll �- I -.--- _ _ .- - ----- _-_-_------- ----. - - - _ - _ _- -_ - - - - -- -- - - _ _ _ -_ __ __ _- __ _- _ _ _ _ _- - -_ -_-_ _ -_ _ _ _ -_ _ _ _- - - -_y_.- -i-----� - - .a- •� -- ._ -- -- - - -- -. ___ ___ ____ ____ ___ ____ _ ___ ____ ____ ___ ____ ___ - --. - - .- -. _ - -_ _ _ _ -_ _ _- -_ -_ _ --.-_- -- ----i--- n: r i -- ---- --- ---- ---- I ' TO FREEZE UN fi _- _--1 L. ii I II I fi CTAULIC NXT REACDON SALVE [j SPRINKLER PLA I j • I i II I I• I I •I I II I SECOND F i OOR FIRST FLOOR HIGH CEILING m Aft Remote Area 5 Fl.M.,Head, 41 Start Head PS 7.06 Wet/Dry WET Density 0.250 Start Mead GPM 21.3 - Hamrd CLASS 1 Area 2600 SOFT per Head 120 Coda NFPA 13 Len/1Wd Ratio 1.20 Elev-Hd to Risar(')408 Construction Max Velocity 15.5 PS-Hd to Riser 14.7 PRESSURE RELIEF VALVE Source Noma or Location Source _/AS REQUIRED FOR GRIDDEO P9 Aw0 al Source 62.5 GPM Req'd at Source INN Iimide Hasa 0.000 HYDRAULIC CALCULATIONS INCLUDE SYSTEMS PER NFPA 13 PSI Req'd at Source 524 IOurali.n .(Source (.000 Outside Hme 500 2500 SQUARE FEET IN CEILING SPRINKLERS PREFER. FROM R TE Safety PS 10.1 Req'd Source Volume (LOGO AND 2 LEVELS OF IN RACKS 5 SPRINKLERS BRANCH LINE Pressure IAwIlobla Pressure of 62.5 psi Exceeds Required Pressure of 524 psi FROM EACH LEVEL Summary This is a safety margin of 10.1 psi or 16 S of Supply ♦3 Atlwnced Max Density Available 0.273 PS lass- TOR to Saurce 11.2 0 Summary I GPM at Max Awllable Density 1638 [Rack Demand 0.1100 Mar"� 1' TEST VA IN- ACCESSIBLE LOCATION TEST AND DRAIN AGF MODEL 1011A (OR SIMILAR) N 10 11 12 13 14 90'ELBOW THROUGH WALL TO \ O4ELUT_E W/CORROSION RES. OUTLE(E0. TO SPRINKLER -----80 0 ------f. rvz ---I ---- WET PIPE SYSTEM TEST CONNECTION 6, -E o 90 "� I x t� [ a 73 5 68 [ 62 55 I ,2]'_ _27'I I -27'. I 101 [ j I I 37'. -IF Y, I 3T, 437' I 37.1 -437 it I I 86 I I - I I w g 37-I0 DECK j FROZEN n 60 STORAGE 56 fi9 I fi3 d 56 I I I I I h P138 J AD ® „leasecall - 4 A3 - I A2 - At - I II I II , e] IIm , IL IL I 30-] DECK A r d ---t I� --------_-_- UPPER LEVEL ACK INKL }9 9 1 5] 6 2 JO 4•$ 64 h 9 2 51 ,A �J I I I I I FROM PAUTIZiNG A 1y y e A v) II 83 OM 6 FEED MAI 5E3 . b I II I I 3J1 a &! I I I45-1 6 CONTROL VALVE N1TH TAMEEO PER SW1T 5E� I 0 A •r rp rp I el •p I I •A ap I 103 aP I ~ g 6 NCTAWC NXi PPEACTION VALVE WITH TRI > n - ---_-_ _ _- _--------_ -------.- -_-- --- -_ _-_--- _-_-_-_- A 6 BUTIERRY VALVE --slot- j ARi TO flE' N AS I --�- ----- -- E%IS 1 G SPft PEERS THIS � �EXIS C SPRI AREJ TO RE A N AS 13 I I 11 0 REM AS j j I j T IN C I I I j N IN CSa ACT Sa " PRE-ACTION SYSTEM SCHEMATIC FREEZER CEILING SPRINKLERS FREEZER UPPER LEVEL RACK SPRINKLERS FREEZER LOWER LEVEL RACK SPRINKLERS Imo IN_y a SUBMITTAL DRAWING 9-25-2012 2' 6' B' 12' 6 16' SPRINKLER DATA REVISIONS Misc. e = 592 CENTER ST P E. SPRINKLER PLAN NORTH SYMBOL SPRINKLER TYPf N.P:T. K FACiOR 7FMP. RARNC AIFGR. MODfC N0. WANRTY DESOR PTTON BY DATE �Q �� �� � � ��� 0• NEW CHROME PENDENT 1/2" 5.6K 155+ WKING WJ18 57 - - PO BOX 582 VC %!/GLI/�/ G� i PIPING PLAN ® EXISRNG CHROME PENDENT 1/2" 56K 155+ ----- ----- 55 SHOWN REVISED 9PRINMR HEADS - CHANGED TO FUSIBLE ❑NK KPL 10-6-12 APPROVAL LOCAL FIRE DEPT LUDLOW, MA. ` O NEW BRASS UPRIGHT 3/9" B.OK 155+ WKING WCJS/ 127 REVISED CALC9 FOR AREAS 1 AND 2 TO REFLECT KPL 10-5-12 - DRAWN BY KPL W ' E ® NEW EXTENDED COVERAGE CHROME PENDENT 3/4' 11.2K 155+ WKING W57J 14 11.2K FUSIBLE LINK EXT COV SPRINKLERS SCALE 1/8"=1'-O' C NEW EX7ENDED COVERAGE BRASS UPRIGHT J/4" 11.2K 155+ WKING N(5J5 24 Fig 589-0672 50 TALBOT LANE DATE 9-25-12 OS NEW EXIENOED COVERAGE CHROME PENDENT J/4' I1.2K 155+ WKING VK573 58 REV DATE a NEW EXTENDED COVERAGE BRASS UPRIGHT 3/4 11.2K 155+ WKING W535 58 MA LIC: SC14712 SOUTH WINDSOR, CT 06074 S - SPRINKLER TOTAL JJ8 NEW ' Expires 4A/2013 FP 2 of 2 I i I i i I i i I I I I MICH PIPE SUPPORT TO SDUCIM.STEEL EXISTING - I�- I MAIN FLOW SNITCH � �-%T 4 DISP) Ll -7�1`fi-7, - 52 I FOOPA loe - B'11 - - - - - Remote Area 4 Flowing Head. 16 Start Head PSI 28.1 KITEFLLTT— I • I p A -°,iyNUES EXISTING RemoteI Wet/Dry WET Density 0.100 Start Head GPM 37.0 1r4 F __ , I h- -- - ALARM VALVE No old LIGHT Arco I500 SOFT per Head 330 it - 106" '1D$ •DISH 10 • - BPNiCNDINE WITH TRIM Coda NFPA 13 Len d Ratio 1.20 ElewHd to Riser 920 ^- SPPoteUR BRANCH UIIE S...o Nixon. Max Velocity I3.7 PSI-Hit to Riser 3.32 - I e Al I - INK UN AI EXISTING I - - I'DROP.IFHGIII VAAIES. III r38 I I Sr 2' I NEW 6' ALARM VALVE Source o a Location Sourcv ']9 _ �II WDOEN 1B'-10)4' fi' BUTTERFLY VALVES PSI Ave al Source 12.1 GPM Req'd al Source 304 In,ide Hose 0.000 '� t I . I�• D2 ROOl1 • WIN TAMPERS 'III( NEW fi'BUTTERFLY VALVE PATH PSI solely PS of Source 44.9 R,q'dS of Source 0000 IOuUida Hava IW I -in LTD r-0 109 1IN b. - - - I III REDUCING ELBOW Salaty P51 44.9 fteq'd Source Volume 0000 "I 110 11 t ® ® TAMPER SW(2 TYPICAL) Pressure IAwOobla Pressure of 823 psi Exceed,Required Pressure of 37.4 pet 1- [Dill - n4CIC TRIO 2"2i I 4" THROUGH WALL TO FDC Summery This is a safely margin of 44.9 psi a 55 X of Supply r-- -- --Q-- - 0- 491 Adwnced Mox Density Awllaele 0.148 PSI be.-TOR to Source 3.80 Ili 1. LAIN- r - 50 49 _ STAINLESS S EL PIPING STMaESS MEL FLEXIELESummery GPIA al Max Awlloble Oeneity 569 IRack Demand 0.000 A - i1 tt2 111 D3 P __ - NDER EOVIP ENT PLATFOR S1RdllXIB1 GDNIEGDDII. -� ' W RELOCATED 4' CHECK VALVE _ I FLEXIBLE CONNECTION r i.. 44 AS __ , P. OD =CE5SROO .t0 EXTENDED REDUCER PEMOVE EXISTING ELBOW AND AVID NEW iEE EXISTING EX STING- B' 3' ER S S 2 UP TO ROO 8'FlPESERNCE _-_-_--------.- __O -- - SEE HIGH CDLI L_- - IUP COUIIC PNIEL 0 5I- -IS4-Y�f'3 6 TPt-, •T =c' NO A.S. -I �" - EN O FlIC ,� II IV_ NKNIS p14B - - 'I4 LE n I HI H CEWN000R � SEE "IS FOR CODING WET RISER DETAIL 5-2 -a�, I FOR COVERAGE IN PRIMER HEAD SEE 1.6'-9'� R. NO SCALE THIS AREA UILARGED DEAL-E THIS UST NKLERCEIRIC EAD 1FE BY II"I fill 6'TO 8'MGM -�3' I ]n - i - -y i ORAWWG. CENTER OF SUPPORT TEE A6 INDICATED,� 8'FAOM 3f : OL/OC es IAg66l DROP TO IMP CEILING DETAIL SCALE: NONE Yy 19--- 11 FI I ./1-�--- ------- 4'" I. lOG1E PEIIOUR SPRUIXLFA NFADS W1111UI fi'TO 9'6[UTTER CDWIC GP10 TEE S3 S3 INK M ,— - I - , TYPICAL FOR PROCESS ROOM N N A I N I I A - ,1 EC NE 3I TO EXI TING 3 - - -_-_- -- _-_-_-_- - - - - �Imo' 1 I- CASs TEE Itf TH PLUG i A - - - OA OC -- 1' L'•- ?" -L .1 PI 7 I I DRY PENDENT SPRINKLER BARREL 7 9 - 6-N, 1V- 10.5 _L J O} } -4 I -� a I i lYCO MODEL OSB-I AIlS - 10 NEW PflOCES EW ADDI 0 PALLETIZING FROZEN DRY SPRINKLER BOOT AREA OF WORK RA L - _ i OFFICES ROOM ROOM FP AA77 STORAGE E INSTALLED PER LISTING A ST I I --- FREEZER/COGLER COILING i III 111 I II I I 1 I f i ===i I I I I I I I I lle -- 2-fi o- 3-s ' �___i i I II I I 11 II 1 1 1 I 1 ESCUTCHEON . NKLER I ISTIN i i I III I I I I I I 6iH MENDED BARREL I- 1 — Ea -1, a c _ . I,^.__, I I I I I I aS REGUIRED I I I I I I I --_-_-- DRY PENDENT INSTALLATION DETAIL I OPEN FEE I NO SCALE — as NG LJ I I I I I I I / EOILFT' BUI LNG 1 u u I_J r COP r. _ 1 �'' / C--- L---- ^r n- — WIL- -e -- 4 7 i, EXI ,... 1 / I %IBTING RIN `ER81 IS REA REMAI J ASrI I 1 EX15i v{b I N-CON -N T I CONTRACT ' I OO ' I I I I O I _ _ t -t .. t I -i' GLOBE VA 7 Ik. ,-- 71 113 EA-I I KITCHE �FER NdE _�X� �2 X 1 REDUCING W I 72! I Fs I I ' COUPLING ❑- %IS 1 -- ---- --- WATER SUPPLY DATA N PIPE NIPPLE _2 X I REDUCING ---_-_- 1-op, ) RESIDUAL fib P51 AI / T ' STATIC: 84 PSI COUPLING EN PLACE \ - 19 L3 V u " - I I ( ) FLOW: 1280 GPM -T' GLOBE VA B.� lo-o l9 3.9.:•..3-n ,.� o-, r IFe EXISTING CITY MAIN DATE 7-10-72 _- _ -_ _ _ -_ _• • �` • ✓', • I �I' PLUG _41 TYP. DRUM DRIP' ASSMEI. y vEs I C EXIST R ( ---- I ( ) THIS IS A DIAGRAMMATIC SITE PLAN. DRY SYSTEM AUXILIARY DRAIN ITS INTENT IS TO SHOW NODE POINT SITE PLAN R°ELAn„O THTHE TREET1"°5 ENS %Isr I NO SCALE SMALL ROOM RULE ------ DENOTES EXISTING SPRINKLER PIPING. IN ACCORDANCE MEN NFPA-13 2007 SECTION jv f%I e s- d 6 t I s I I I DENOTES NEW SPRINKLER PIPING. SPRINKLERS SHALL SHALL BE PERMITTED TO BE LOCATEOMS AS DEFINED IN D -.-. -_- NOT MORE THAN 9 FT. FROM ANY SINGLE WALL-. �/ .-.-_-_— P III ICE1 d ILENE S L KE s I — 2 2 ( I SPRINKLER SYSTEM GENERAL NOTES P. t• ' 1 A AFCON FlG. 310 SURGE flESTRAINER 1 6 N TYPE 1 - FOR 3/4"AND 2' PIPE AND HANGER TYPE 2 - FOR 2-1/2' AND 3- PIPE AND HANGER _.-.- _ - _ __ + • •X -ALL PIPING 1"-1 1/2" IS BLACK SCHEDULE 40 THREADED FOR USE WITH STANDARD WIT. ELK CI SCREWED FITTINGS. C OS f PERKS S %IS 18 I •' • - •'' • enR e01s7 -ALL PIPING 2Yq" AND LARGER IS BLACK SCHEDULE 10 ROLL GROOVED FOR USE WITH MECH. TEES & GROOVED FITTINGS fitE EXIST DRY `II I G M 1/2' NUT -ALL FREEZER PIPING TO BE GALVANIZED SCHEDULE 10 ROLL GROOVED FOR USE WITH MECH. TEES & GROOVED FITTINGS 1 - - DO A - -- a 1- --3'FlSH PurE -PLATFORM PIPING AND HANGERS ARE TO BE AS FOLLOWS: FEED SHALL BE FROM OVERHEAD SPRINKLER SYSTEM FOR THE AREA PLATFORM IS IN. LLI4 Y 1 ® TRANSITION TO STAINLESS STEEL APPROXIMATELY 12'ABOVE IMP CBUNG. SPRINKLER PIPING DROP TO BELOW IMP CDUNG AND PIPE LOCATED BELOW PLATFORM SHALL BE 304 STAINLESS STEEL WITH A316 STAINLESS STEEL FIT➢NGS OR SHALL BE 304 SOCKET WELDED. HANGERS AND SUPPORT SHALL BE D G IT i EXIS RESTRAIN THE UPWARD MOVEMENT OF PIPE --3`FSH PLATE STAINLESS STEEL. SUPPORT RODS SHALL BE END THREADED STAINLESS SUED.SMOOTH RODS. HANGERS AND SUPPORTS SHALL BE WELDED TO PLATFORM.All AND CONK CT TO 8 I X AS IT OCCURS DURING SPRINKLER HEAD WELDS SHALL BE CONTINUOUS, GROUND SMOOTH,AND FREE OF ANY DISCOLORATION. M •'' /I ACTIVATION OR SEISMIC ACTIVITY 1/2'NUT ROD -ALL HANGERS ARE TO BE A.T. ROO ANO BANG HANGERS. D HPNLE� - - p N M -ALL NEW SPRINKLER DENCES TO BE U.L. LISTED AND/OR FM APPROVED FOR SPRINKLER SYSTEMS. ALL ILK PIPIRG IS SIZED PER HYDRAULIC CALCULATIONS. wi • A 1 I Atz I 1- --@ e^++D ® 8'MAIN -HYDRAULIC CALCULATIONS HAVE BEEN BASED ON A FLOW TEST DATA OF 84 P51 STATIC, 68 PSI RESIDUAL, ANO 1280 GPM FLOW. HN GER I1 IT try I I - ® DENOTES HYDRAULIC REFERENCE POINT F9 Flp, , I-P 2-0 I TI m 'j o-e" -THIS SYSTEM HAS BEEN DESIGNED AND WILL BE INSTALLED PER ALL STATE AND LOCAL CODES AND NFPA PAMPHLET 13. _ I I I I -LOCATION OF ALL HIGH TEMPERATURE SPRINKLERS TO BE DETERMINED IN FIELD. - E — —' F :mil„ Ib I amm,on Be.Chump — -SPRINKLERS ARE REQUIRED TO BE CENTERED IN CEILING TILES WHERE POSSIBLE. A I A=•ie -THIS SYSTEM WILL BE TESTED IN ACCORDANCE WITH NFPA 13. (MwW Kuhu&NvBen I 1bp&BOltom\ •^*'a ru,oae / \ l \ FREEZER TO PROVIDE HEAT THROUGH OUT ENTIRE BUILDING TO PREVENT FREEZING OF SPRINKLER PIPES, WITH EXCEPTION TO THE FREEZER SPACE. /I ,m_am o,...we nms m-nwro s...•ual ,'rtmo ua1-sw1J ATI -ALL PRE-ACTION SYSTEM PIPING IS TO BE PITCHED TO ALLOW FOR DRAINAGE. BRANCHLINES TO BE PITCHED Yj PER'10'-0". Oxxi0b) CROSSMAINS TO BE PITCHED Y" PEft 10'-0'. 1' X ARMOVER I I I Nvayer Wa. (SEE PLAN) I -5 I ISTI G S RINK RS I THIS w.r L , - SCOPE OF WORK. AREA O;ON AS I (,�TI7 '6'unww 1' 90 EL I I .p� 19•- -INSTALLATION OF A WET TYPE FIRE SPRINKLER SYSTEM TO PROTECT THE NEW ADDITION EW 6 ALARM VALVE RISE to T 18 I I NO ICONTRAC LATERAL SWAY BRACE LONGITUDINAL SWAY BRACE t'X D'-2' NIPPLE. 1pI� WITH NON-THREADED FITTINGS WITH NON-THREADED FITTINGS -INSTALLATION OF A PRE-ACTION TYPE FIRE SPRINKLER SYSTEM TO PROTECT THE NEW FREEZER 1' % DROP .+3- Y il-Ih e N I I LATERAL SPACED 0 MAX OF 40' LONGITUDINAL SPACED AT Rote trap EXISTING s ALARM VALVE TO REMAIN - - P3-3,5 -WORK TO START AT THE EXISTING 6' WET RISER. A NEW ALARM VALVE WILL BE ADDED. THE NEW ALARM VALVE RISER WILL FEED —(SEE PLAN) - ---- I SHALL BE PROVIDED A MAX. OF 80' SHALL BE THE EXISTING OFFICE SPACE, THE NEW OFFICE SPACE (FIRST AND SECOND FLOORS) AND THE REMAINDER OF THE NEW ADDITION, BRANCHUNE- W I I LK-ON FOR ALL FEED AND CROSSAIAINS, PROVIDED ON FEED & CROSS /1' x t/2'R.C. "1 I I I I REGARDLESS OF SIZE, WITH MAINS PER NFPA 13 SEC. 9.3.5.4 INCLUDING THE NEW FREEZER.. All crt'S+1'• HANGER ROD LONGER THAN 6" Beam Chump PENDENT RA ESCL I Y MAIN -$-- PER NFPA 13 SECTION 9.3.5.3 MISC. NOTES SUSPENDED CEIUNG� XI I _ _-_ _- -_ _ p m (�>wth) T = TWO-WAY EARTHQUAKE BRACE -BUILDING CONSTRUCTION IS OF NON-COMBUSTIBLE STEEL JOIST CONSTRUCTION WITH STEEL DECK = RISER EARTHQUAKE BRACE Hower� -BUILDING OCCUPANCY: LIGHT HAZARD - OFFICE AREAS ORDINARY HAZARD GROUP 2 - PALLETIZING AREA, PACKAGING ROOM, AND PROCESS ROOM. A FRIGFFATIQN I _ CLASS 1 - FROZEN STORAGE SPRINKLER HEAD DETAIL I %PANAON SEISMIC HANGER DETAIL FOR NEW PIPING ONLY - PI90 I -SPRINKLER SPACING: LIGHT HAZARD AREAS - MAX 225 SOFT. (TYPICAL FOR ALL NEW ARMOVERS I LAP 9 SEISMIC BRACING ORDINARY HAZARD AREAS - MAX 130 SOFT. USING EXISTING 1' OUTLETS.) I I HANGER DETAILS CLASS 1 - MAX 100 SF • • -FREEZER DESIGN CRITERIA SHALL BE .26 GPM OVER THE REMOTE 2600 SQUARE FEET AT THE CEILING SPRINKLER LEVEL AND SHALL PROVIDE 30 GPM OVER 10 IN RACK SPRINKLERS. (5 IN RACK SPRINKLERS PER LEVEL). SEE CONTRACT DRAWINGS FOR FURTHER DESIGN CRITERIA INFORMATION. (NFPA 13 TABLE 16.3.1.1 AND TABLE 16.3.1.2) FIRST FLOOR PART PLAN SUBMITTAL DRAWING 9-25-2012 2 fi' 6' 10' 12' „' 16' ,B' SPRINKLER DATA REVISIONS MISC. 592 CENTER ST P.E. SPRINKLER PLAN NORTH SYMBOL SPRINKLER TYPE N.P.T. K FACTOR TEMP. RA BNB AIFGR. MODEL NO. 0UANRTY DESCRITMON BY DARE A v/�7( O NEW CHROME PENDENT 1/2' 5.6K 155• WKING VKJ78 57 PO BOX 582 (//�J V PIPING PLAN ® EXISTING CHROI4£PENDENT 1 2" 5.6K 155e ----- ----- 56 SHOWN REVISED 9PITINIQER HEADS - CHANGED 70 PU9®LE LINK KPL 10-6-12 (�f APPROVAL LOCAL FIRE DEPT O NEW BRASS UPRIGHT J/4" 8.OK 155• WKING WYJ51 127 LUDLOW, MA. W �� E N NEW EX71FAVED COVERAGE CHROME PENDENT J/4" 11.2K 155• DIVING W57J 14 11R�2K eFUSIBLE LORE EXT COV SPRINKLERS SCALE I(PL 10-6-12 DRAWN BY 1/B"=1'-O' * NEW EXTENDED COVERAGE BRASS UPRIGHT 3/4" I1.2K 155e MONG w5J5 24 ® (413) 589-0672 50 TALBOT LANE DATE 9-25-12 01 NEW EXTENDED COVERAGE CHROME PENDENT J/4' 11.2K 155• WKING W573 58 REV DATE 10-5-12 S Os NEW EXTENDED COWRAGE BRASS UPRIGHT J/4' I1.2K 155• WKING W535 58 MA LIC: #SC14712 SOUTH WINDSOR, CT 06074 SPRINKLER TOTAL JJ8 NEW t Expires a 21/2013 FP 1 of 2 CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:46 HYDRAULIC DESIGN INFORMATION SHEET Job Name: CARLAS PASTA Location: 50 TALBOT LANE SOUTH WINDSOR, CT. 06074 Drawing Date: 9-21-12 Remote Area Number: ] Contractor: LEGACY FIRE PROTECTION, INC. Telephone:413 589-0672 592 CENTER STREET PO BOX 582 LUDLOW, MA. 01056 Designer: KPL Calculated By:SprinkCAD www.sprinkcad.com 451 N. Cannon Ave. Lansdale, PA 19446 Construction: STEEL JOIST Occupancy:BAKERY Reviewing Authorities:LOCAL FIRE DEPT SYSTEM DESIGN Code:NFPA 13 Hazard:ORDINARY 2 System Type:WET Area of Sprinkler Oper. 1500 sq ftj Sprinkler or Nozzle Density (gpm/sq ft) 0.200 1 Make: Tyco Area per Sprinkler 255.0 sq ftj Model: EC-11 Hose Allowance Inside 0 gpm I K-Factor:11.20 Hose Allowance Outside 250 gpm I Temperature Rating: 155 CALCULATION SUMMARY 9 Flowing Outlets gpm Required: 721.0 psi Required: 48.4 @ Source WATER SUPPLY Water Flow Test Pump Data Date of Test 7-10-12 1 Rated Capacity 0 gpm Static Pressure 84 .0 psi I Rated Pressure 0.0 psi Residual Pres 68.0 psi I Elevation 0 At a Flow of 1280 gpm I Make: Elevation 0" I Model: Location: ON SITE Source of Information: CONTRACT DRAWINGS SYSTEM VOLUME 2111 Gallons Notes: GRID PEAKED CURRENT LOCATION REQUIRED 48.432 psi 720.99 gpm SHIFT LEFT (DOWN) REQUIRED 48.406 psi 735.36 gpm SHIFT RIGHT (UP) REQUIRED 48.420 psi 720.93 gpm CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:46 HYDRAULIC CALCULATION DETAILS HYDRAULIC FLOW LOSS QTY DESCRIPTION LENGTH C ID gpm psi TOTALS Hydr Ref W Required at Hyd Area 1 471 44.2 psi 1 6" Grvd Alarm Valve 32' 120 6. 065 471 0.3 1 6" Grvd Butterfly Valve Tyco BFV- 11' 120 6.065 471 0.1 1 6" Fingd Back Flow Valve Ames 200 CHART LOSS 471 2.3 1 8" x 6" Fingd 90 Ell CI 18 ' 120 8. 071 471 0.0 Elevation Change 310" 1.3 1 Pipe 8" DIx18 America DI 350 100' 140 8 .488 471 0.1 2 8" MJ 90 Ell DI 48' 120 8. 071 471 0.1 1 8" Fingd Gate Valve Kennedy Gate 8' 120 8.071 471 0.0 1 8" MJ Tee DI 24 ' 120 8 .071 471 0.1 Fixed Flow Flow Loss 250 gpm Hydr Ref R1 Required at Source 721 48.4 psi Water Source 84 .0 psi static, 68.0 psi residual @ 1280 gpm 721 gpm 78.5 psi SAFETY PRESSURE 30.0 psi Available Pressure of 78.5 psi Exceeds Required Pressure of 48.4 psi This is a safety margin of 30.0 psi or 38 % of Supply Maximum Water Velocity is 9.3 fps 3: CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:46 Page 3 FITTING NAME TART-,R ABBREV. NAME C Coupling E 90' Standard Elbow F 45' Elbow S Straight Flow Thru Tee T 90' Flow Thru Tee V Valve LEGEND HYD REF Hydraulic reference. Refer to accompanying flow diagram.K FACTOR Flow factor for open head or path where Flow (gpm) = K x -\/_P Qa Flow added or subtracted Qt Total flow DIA Actual internal diameter of pipe C Hazen Williams pipe roughness factor Pf/ft Friction loss per foot of pipe PIPE Length of pipe FTNG'S Number of fittings. See table above. TOTAL Total length (PIPE + FTNG'S) Pt Total pressure (psi) at fitting Pe Pressure due to change in elevation where Pe = 0.433 x change in elevation Pf Friction loss (psi) to fitting where Pf = 1 x 4.52 x (Q/C) ^1.85 / ID^4 .87 Pv Velocity pressure (psi) where Pv = 0.001123 x Q^2/ID^4 Pn Normal pressure (psi) , where Pn = Pt - Pv NOTES: - Pressures are balanced to 0. 01 psi. Pressures are listed to 0.1 psi. Addition may vary by 0.1 psi due to accumulation of round off. - Calculations conform to NFPA 13. - Velocity Pressures are not considered in these Calculations CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:46 Page 4 NODE ELEVATION SPRINKLER NUMBER K-FACTOR FLOW FLOW DENSITY (FT) (GPM/ (PSI^1_2) ) (PSI) (GPM) (GPM) (GPM/SQ.FT) 1 29.50 20.7 1S 29.50 11.20 20.7 51.0 51.0 0.20 2 29.50 20.7 2S 29.50 11.20 20.7 51.0 51. 0 0.20 3 29.50 30.1 3S 29.50 11.20 30.1 61.5 51.0 0.24 17 29.50 21.1 17S 29.50 11.20 21.1 51.4 51.0 0.20 18 29.50 21.0 18S 29.50 11.20 21.0 51.3 51.0 0.20 19 29.50 20.7 19S 29.50 11.20 20.7 51.0 51.0 0.20 21 29.50 21.1 21S 29.50 11.20 21.1 51.4 51.0 0.20 22 29.50 21.0 22S 29.50 11.20 21.0 51.3 51.0 0.20 23 29.50 20.7 23S 29.50 11.20 20.7 51.0 51.0 0.20 104 29.50 22.2 A9 29.50 31.2 A10 29.50 31.7 All 29.50 31.7 Al2 28.00 32.7 A13 3.00 44 .1 Cl 29.50 31.1 C2 29.50 31.1 C3 29.50 31.1 C4 29.50 31.2 E1 29.50 31.7 E2 29.50 31.7 E3 29.50 31.7 E4 29.50 31.7 E5 29.50 31.7 E6 29.50 31.7 F1 28. 00 32.9 W 3.00 44 .2 Max velocity of 9.30 occurs in the pipe from E3 TO 21 Nodes with "S" indicate a node at the top of a sprig or bottom of drop pendent. The node without an "S" is on the branch. CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:46 Tyco Fire Products Page 5 HYD. Oa REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* POINT Qt Pf/ft TOTAL Pf Pn PATH 1 FROM HYDRAULIC REFERENCE 19 TO W (PRIMARY PATH) 51 .00 1.049 1T 0.00 20.7 20.7 K = 11.20 19S C=120 0.00 0.0 0.0 51 . 00 0.735 0.00 0. 0 20.7 Vel = 19.12 2.157 14 .00 20.7 20.7 EqK = 11.20 19 C=120 0.00 0.0 0.0 48.56 0.020 14 .00 0.3 20.7 Vel = 4 .31 51.34 2.157 1T 120.17 21.0 21.0 EqK = 11.20 18 C=120 12.31 0.0 0.0 99. 90 0.076 132.48 10.1 21.0 Vel = 8 .86 6.357 14 .00 31. 1 31.1 Cl C=120 0.00 0. 0 0.0 99. 90 0. 000 14 .00 0.0 31.1 Vel = 1.02 99. 91 6.357 14 .00 31. 1 31.1 C2 C=120 0.00 0. 0 0.0 See PATH 3 199.82 0.001 14 .00 0.0 31.1 Vel = 2.04 27 .59 6.357 14 .00 31.1 31.1 C3 C=120 0.00 0.0 0.0 See PATH 6 227 .40 0.002 14 .00 0.0 31.1 Vel = 2.32 -13.50 6.357 1T 2.71 31.2 31.2 C4 C=120 37.72 0.0 0.0 See PATH 7 213.90 0.002 40.43 0.1 31.2 Vel = 2.18 6.357 1T 276.73 31.2 31.2 A9 - C=120 37.72 0.0 0.0 213.90 0.002 314 .45 0.5 31.2 Vel = 2.18 257 .09 6.357 0.46 31.7 31.7 A10 C=120 0.00 0.0 0.0 See PATH 2 470. 99 0. 007 0.46 0.0 31.7 Vel = 4 .81 8.249 3E 120.52 31.7 31.7 All C=120 60.05 0. 6 0.0 470. 99 0. 002 180.57 0.4 31.7 Vel = 2.86 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:46 Tyco Fire Products Page 6 HYD REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* POINT Qt Pf/ft TOTAL Pf Pn PATH 1 FROM HYDRAULIC REFERENCE 19 TO W (PRIMARY PATH) 8.249 1E 43.56 32.7 32.7 Al2 C=120 20.02 0.0 0.0 470. 99 0.002 63.58 0.1 32.7 Vel = 2.86 6.357 2E 25.00 32. 9 32.9 F1 C=120 35.21 10.8 0.0 470. 99 0.007 60.21 0.4 32.9 Vel = 4.81 6.357 2.75 44.1 44.1 A13 C=120 0.00 0.0 0.0 470. 99 0.007 2.75 0.0 44.1 Vel = 4 .81 W 470. 99 44.2 K = 70.88 51.34 1.049 1T 0.00 21.0 21.0 K = 11.20 18S C=120 0.00 0.0 0.0 51.34 0.745 0.00 0.0 21.0 Vel = 19.25 18 51.34 21.0 K = 11.20 PATH 2 FROM HYDRAULIC REFERENCE 19 TO A10 51.00 1.049 1T 0.00 20.7 20.7 K = 11.20 19S C=120 0.00 0.0 0.0 51.00 0.735 0.00 0.0 20.7 Vel = 19.12 2.157 13.67 20.7 20.7 EqK = 11.20 19 C=120 0.00 0.0 0.0 2.44 0. 000 13.67 0.0 20.7 Vel = 0.22 51.00 2.157 14 .00 20.7 20.7 EqK = 11.20 2 C=120 0.00 0.0 0.0 53.44 0.024 14 .00 0.3 20.7 Vel = 4.74 51.41 2.157 13.00 21. 1 21 .1 EqK = 11.20 17 C=120 0.00 0.0 0.0 104 .85 0.083 13.00 1.1 21.1 Vel = 9.30 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:46 Tyco Fire Products Page 7 H REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* POINT Qt Pf/ft TOTAL Pf Pn PATH 2 FROM HYDRAULIC REFERENCE 19 TO A10 CONTINUED 2.157 1T 101.89 22.2 22.2 104 C=120 12.31 0.0 0.0 104 . 85 0.083 114 .20 9.5 22.2 Vel = 9.30 6.357 0.88 31.7 31.7 E1 C=120 0.00 0.0 0.0 104 .85 0.000 0.88 0.0 31.7 Vel = 1.07 6.357 13.12 31.7 31.7 E2 C=120 0.00 0.0 0.0 104 . 85 0.000 13.12 0.0 31.7 Vel = 1.07 104 . 86 6.357 1.37 31.7 31.7 E3 C=120 0.00 0.0 0.0 See PATH 4 209.72 0.002 1.37 0.0 31.7 Vel = 2.14 6.357 12.63 31.7 31.7 E4 C=120 0.00 0.0 0.0 209.72 0.002 12.63 0.0 31.7 Vel = 2.14 33. 87 6.357 14 .00 31.7 31 .7 E5 C=120 0.00 0.0 0.0 See PATH 5 243.59 0.002 14 .00 0.0 31.7 Vel = 2.49 13.50 6.357 2.71 31.7 31.7 E6 C=120 0.00 0.0 0.0 See PATH 7 257.09 0.002 2.71 0.0 31.7 Vel = 2. 62 A10 257 .09 31.7 K = 45.64 51.00 1.049 1T 0.00 20.7 20.7 K = 11.20 2S C=120 0.00 0.0 0.0 51.00 0.735 0.00 0.0 20.7 Vel = 19.12 2 51. 00 20.7 K = 11.20 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:46 Tyco Fire Products Page 8 pi REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* POINT Qt Pf/ft TOTAL Pf Pn 51.41 1.049 1T 0.00 21.1 21.1 K = 11.20 17S C=120 0.00 0.0 0.0 51.41 0.746 0.00 0.0 21.1 Vel = 19.27 17 51.41 21.1 K = 11.20 PATH 3 FROM HYDRAULIC REFERENCE 23 TO C2 51 .00 1.049 1T 0.00 20.7 20.7 K = 11.20 23S C=120 0.00 0.0 0.0 51 .00 0.735 0.00 0.0 20.7 Vel = 19.12 2.157 14.00 20.7 20.7 EqK = 11.20 23 C=120 0.00 0.0 0.0 48 .56 0.020 14.00 0.3 20.7 Vel = 4 .31 51.35 2.157 1T 120.17 21.0 21.0 EqK = 11.20 22 C=120 12.31 0.0 0.0 99. 91 0.076 132.48 10.1 21.0 Vel = 8 .86 C2 99. 91 31.1 K = 17.91 51.35 1.049 1T 0.00 21.0 21.0 K = 11.20 22S C=120 0.00 0.0 0.0 51.35 0.745 0.00 0.0 21.0 Vel = 19.25 22 51 .35 21.0 K = 11.20 PATH 4 FROM HYDRAULIC REFERENCE 23 TO E3 51.00 1.049 1T 0.00 20.7 20.7 K = 11.20 23S C=120 0.00 0.0 0.0 51. 00 0.735 0.00 0.0 20.7 Vel = 19.12 2.157 13. 67 20.7 20.7 EqK = 11.20 23 C=120 0.00 0.0 0.0 2.44 0.000 13.67 0.0 20.7 Vel = 0.22 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:46 Tyco Fire Products Page 9 HYD. REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* POINT Qt Pf/ft TOTAL Pf Pn PATH 4 FROM HYDRAULIC REFERENCE 23 TO E3 CONTINUED 51. 01 2.157 14 .00 20.7 20.7 EqK = 11.20 1 C=120 0.00 0.0 0.0 53.45 0.024 14 .00 0.3 20.7 Vel = 4 .74 51.42 2.157 1T 114 .89 21. 1 21.1 EqK = 11.20 21 C=120 12.31 0.0 0.0 104.86 0.083 127.20 10. 6 21.1 Vel = 9.30 E3 104 .86 31.7 K = 18 .63 51.01 1.049 1T 0.00 20.7 20.7 K = 11.20 1S C=120 0.00 0.0 0.0 51.01 0.735 0.00 0. 0 20.7 Vel = 19.12 1 51. 01 20.7 K = 11.20 51.42 1.049 1T 0.00 21.1 21.1 K = 11.20 21S C=120 0.00 0.0 0.0 51.42 0.746 0.00 0.0 21.1 Vel = 19.27 21 51.42 21.1 K = 11.20 PATH 5 FROM HYDRAULIC REFERENCE 3 TO E5 61.45 1.049 1T 0.00 30.1 30.1 K = 11.20 3S C=120 0.00 0.0 0.0 61.45 1.038 0.00 0.0 30.1 Vel = 23.04 2.157 1T 142.56 30.1 30.1 EqK = 11.20 3 C=120 12.31 0.0 0.0 33. 87 0.010 154 .87 1. 6 30.1 Vel = 3.00 E5 33.87 31.7 K = 6.02 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) 7 CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:46 Tyco Fire Products Page 10 HYD REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* POINT Qt Pf/ft TOTAL Pf Pn PATH 6 FROM HYDRAULIC REFERENCE 3 TO C3 61 .45 1. 049 1T 0.00 30.1 30.1 K = 11.20 3S C=120 0.00 0.0 0.0 61 .45 1. 038 0.00 0.0 30.1 Vel = 23.04 2. 157 1T 134 .16 30.1 30.1 EqK = 11.20 3 C=120 12.31 0.0 0.0 27 .59 0.007 146.47 1.0 30.1 Vel = 2.45 C3 27 .59 31.1 K = 4.94 PATH 7 FROM HYDRAULIC REFERENCE C4 TO E6 13.50 2.157 2T 276.73 31.2 31.2 C4 C=120 24.61 0.0 0.0 See PATH 1 13.50 0.002 301.34 0. 6 31.2 Vel = 1.20 E6 13.50 31.7 K = 2.40 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) L ' CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:48 HYDRAULIC DESIGN INFORMATION SHEET Location: 50 TALBOT LANE SOUTH WIND,SOR, CT. 06074 Drawing Date: 9-21-12 Remote Area Number: 2 Contractor: LEGACY FIRE PROTECTION, INC. Telephone:413 589-0672 592 CENTER STREET PO BOX 582 LUDLOW, MA. 01056 Designer: KPL Calculated By:SprinkCAD www.sprinkcad.com 451 N. Cannon Ave. Lansdale, PA 19446 Construction: STEEL JOIST Occupancy:BAKERY Reviewing Authorities:LOCAL FIRE DEPT SYSTEM DESIGN Code:NFPA 13 Hazard:ORDINARY 2 System Type:WET Area of Sprinkler Oper. 1500 sq ftj Sprinkler or Nozzle Density (gpm/sq ft) 0.200 1 Make: Tyco Area per Sprinkler 255.0 sq ftl Model: EC-11 Hose Allowance Inside 0 gpm K-Factor:11.20 Hose Allowance Outside 250 gpm Temperature Rating: 155 CALCULATION SUMMARY 9 Flowing Outlets gpm Required: 746.7 psi Required: 59.6 @ Source WATER SUPPLY Water Flow Test Pump Data Date of Test 7-10-12 Rated Capacity 0 gpm Static Pressure 84 .0 psi Rated Pressure 0.0 psi Residual Pres 68 .0 psi Elevation 0 At a Flow of 1280 gpm Make: Elevation 0" Model: Location: ON SITE Source of Information: CONTRACT DRAWINGS SYSTEM VOLUME 2111 Gallons Notes: CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:48 HYDRAULIC CALCULATION DETAILS HYDRAULIC FLOW LOSS QTY DESCRIPTION LENGTH C ID m gp psi TOTALS Hydr Ref W Required at Hyd Area 2 497 55.2 psi 1 6" Grvd Alarm Valve 32' 120 6.065 497 0.3 1 6" Grvd Butterfly Valve Tyco BFV- Ill 120 6.065 497 0.1 1 6" Fingd Back Flow Valve Ames 200 CHART LOSS 497 2.3 1 8" x 6" Fingd 90 Ell CI 18 ' 120 8.071 497 0.0 Elevation Change 310" 1.3 1 Pipe 8" DIx18 America DI 350 100' 140 8.488 497 0.1 2 8" MJ 90 Ell DI 48 ' 120 8 .071 497 0.1 1 8" Fingd Gate Valve Kennedy Gate 8' 120 8.071 497 0.0 1 8" MJ Tee DI 24 ' 120 8.071 497 0.1 Fixed Flow Flow Loss 250 gpm Hydr Ref R1 Required at Source 747 59.6 psi Water Source 84 .0 psi static, 68.0 psi residual @ 1280 gpm 747 gpm 78.1 psi SAFETY PRESSURE 18.5 psi Available Pressure of 78.1 psi Exceeds Required Pressure of 59.6 psi This is a safety margin of 18.5 psi or 24 % of Supply Maximum Water Velocity is 19.1 fps CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:48 Page 3 FITTING NAME TABLE ABBREV. NAME C Coupling E 90' Standard Elbow F 45' Elbow S Straight Flow Thru Tee T 90' Flow Thru Tee V Valve LEGEND HYD REF Hydraulic reference. Refer to accompanying flow diagram.K FACTOR Flow factor for open head or path where Flow (gpm) = K x -\/_P Qa Flow added or subtracted Qt Total flow DIA Actual internal diameter of pipe C Hazen Williams pipe roughness factor Pf/ft Friction loss per foot of pipe PIPE Length of pipe FTNG'S Number of fittings. See table above. TOTAL Total length (PIPE + FTNG'S) Pt Total pressure (psi) at fitting Pe Pressure due to change in elevation where Pe = 0.433 x change in elevation Pf Friction loss (psi) to fitting where Pf = 1 x 4.52 x (Q/C) ^1.85 / IDA4.87 Pv Velocity pressure (psi) where Pv = 0.001123 x Q^2/IDA4 Pn Normal pressure (psi) , where Pn = Pt - Pv NOTES: - Pressures are balanced to 0.01 psi. Pressures are listed to 0.1 psi. Addition may vary by 0.1 psi due to accumulation of round off. - Calculations conform to NFPA 13. - Velocity Pressures are not considered in these Calculations CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:48 Page 4 NUMBER K-FACTOR FLOW FLOW DENSITY (FT) (GPM/ (PSI^li) ) (PSI) (GPM) (GPM) (GPM/SQ.FT) 1 29.50 30.4 1S 23. 00 11.20 23.7 54 .5 51.0 0.21 2 29.50 30.7 2S 23.00 11.20 23.9 54 .7 51.0 0.21 3 29.50 41.0 3S 23.00 11.20 31.4 62.7 51.0 0.25 4 29.50 30.8 4S 23.00 11.20 24.0 54 .8 51.0 0.22 5 29.50 26.4 5S 23.00 11.20 20.7 51.0 51.0 0.20 17 29.50 30.7 17S 23.00 11.20 23.9 54.7 51.0 0.21 18 29.50 32.0 19 29.50 30.9 19S 23.00 11.20 24.0 54 . 9 51.0 0.22 21 29.50 30.4 21S 23.00 11.20 23.7 54 .5 51.0 0.21 22 29.50 31.7 23 29.50 30.7 23S 23. 00 11.20 23.8 54.7 51.0 0.21 104 29.50 31.1 A9 29.50 42.1 A10 29.50 42.7 All 29.50 42.7 Al2 28.00 43.7 A13 3.00 55.2 Cl 29.50 42.0 C2 29.50 42.0 C3 29.50 42.1 C4 29.50 42.1 E1 29.50 42.6 E2 29.50 42.6 E3 29.50 42.6 E4 29.50 42. 6 E5 29.50 42.6 E6 29.50 42.7 F1 28.00 43.8 W 3.00 55.2 Max velocity of 19.12 occurs in the pipe from 5 TO 104 Nodes with "S" indicate a node at the top of a sprig or bottom of drop pendent. The node without an "S" is on the branch. CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:48 Tyco Fire Products Page 5 REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* POINT Qt Pf/ft TOTAL Pf Pn PATH 1 FROM HYDRAULIC REFERENCE 5 TO W (PRIMARY PATH) 51.00 1.049 lE 6.50 20.7 20.7 K = 11.20 5S C=120 5.00 -2.8 0.0 51 .00 0.735 11.50 8.4 20.7 Vel = 19.12 1.049 1T 1.50 26.4 26.4 EqK = 9.93 5 C=120 5.00 0.0 0.0 51 .00 0.735 6.50 4.8 26.4 Vel = 19.12 64 .78 2.157 1T 101.89 31.1 31.1 104 C=120 12.31 0.0 0.0 See PATH 5 115.78 0.100 114.20 11.4 31.1 Vel = 10.26 6.357 0.88 42. 6 42.6 E1 C=120 0.00 0.0 0.0 115.78 0.001 0.88 0.0 42.6 Vel = 1.18 6.357 13.12 42. 6 42.6 E2 C=120 0.00 0.0 0.0 115.78 0.001 13.12 0.0 42.6 Vel = 1.18 117.56 6.357 1.37 42.6 42.6 E3 C=120 0.00 0.0 0.0 See PATH 3 233.34 0.002 1.37 0.0 42.6 Vel = 2.38 6.357 12.63 42.6 42.6 E4 C=120 0.00 0.0 0.0 233.34 0.002 12.63 0.0 42.6 Vel = 2.38 34 .44 6.357 14 .00 42. 6 42.6 E5 C=120 0.00 0.0 0.0 See PATH 6 267.78 0.002 14 .00 0.0 42.6 Vel = 2.73 13.58 6.357 2.71 42.7 42.7 E6 C=120 0.00 0.0 0.0 See PATH 8 281.36 0.003 2.71 0.0 42.7 Vel = 2.87 215.29 6.357 0.46 42.7 42.7 A10 C=120 0.00 0.0 0.0 See PATH 2 496. 65 0.008 0.46 0.0 42.7 Vel = 5.07 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:48 Tyco Fire Products Page 6 REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* POINT Qt Pf/ft TOTAL Pf Pn PATH 1 FROM HYDRAULIC REFERENCE 5 TO W (PRIMARY PATH) 8.249 3E 120.52 42.7 42 .7 All C=120 60.05 0.6 0.0 496. 65 0.002 180.57 0.4 42.7 Vel = 3.01 8.249 lE 43.56 43.7 43.7 Al2 C=120 20.02 0.0 0.0 496. 65 0.002 63.58 0.1 43.7 Vel = 3.01 6.357 2E 25.00 43.8 43.8 Fl C=120 35.21 10.8 0.0 496. 65 0.008 60.21 0.5 43.8 Vel = 5.07 6.357 2.75 55.2 55.2 A13 C=120 0.00 0.0 0.0 496. 65 0.008 2.75 0.0 55.2 Vel = 5.07 W 496.65 55.2 K = 66.86 PATH 2 FROM HYDRAULIC REFERENCE 1 TO A10 54 .48 1.049 1T 6.50 23.7 23.7 K = 11.20 1S C=120 5.00 -2.8 0.0 54 .48 0.831 11.50 9.5 23.7 Vel = 20.42 2.157 13.67 30.4 30.4 EqK = 9.88 1 C=120 0.00 0.0 0.0 46.26 0.018 13.67 0.3 30.4 Vel = 4 .10 54. 69 2.157 14 .00 30.7 30.7 EqK = 9.88 23 C=120 0.00 0.0 0.0 100. 96 0.078 14 .00 1. 1 30.7 Vel = 8 .95 2.157 1T 120.17 31.7 31.7 22 C=120 12.31 0.0 0.0 100. 96 0.078 132.48 10.3 31.7 Vel = 8.95 99. 61 6.357 14 .00 42.0 42.0 C2 C=120 0.00 0.0 0.0 See PATH 4 200.57 0.001 14 .00 0.0 42. 0 Vel = 2.05 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:48 Tyco Fire Products Page 7 REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* POINT Qt Pf/ft TOTAL Pf Pn PATH 2 FROM HYDRAULIC REFERENCE 1 TO A10 CONTINUED 28 .30 6.357 14 .00 42.1 42.1 C3 C=120 0.00 0.0 0.0 See PATH 7 228.87 0. 002 14 .00 0.0 42.1 Vel = 2.34 -13.58 6.357 1T 2.71 42.1 42.1 C4 C=120 37 .72 0.0 0.0 See PATH 8 215.29 0.002 40.43 0.1 42.1 Vel = 2.20 6.357 1T 276.73 42.1 42.1 A9 C=120 37.72 0.0 0.0 215.29 0.002 314 .45 0.5 42.1 Vel = 2.20 A10 215.29 42.7 K = 32.96 54. 69 1.049 1T 6.50 23.8 23.8 K = 11.20 23S C=120 5.00 -2.8 0.0 54 . 69 0. 837 11 .50 9. 6 23.8 Vel = 20.50 23 54.69 30.7 K = 9.88 PATH 3 FROM HYDRAULIC REFERENCE 1 TO E3 54 .48 1.049 1T 6.50 23.7 23.7 K = 11.20 1S C=120 5.00 -2.8 0.0 54 .48 0.831 11.50 9.5 23.7 Vel = 20.42 2. 157 14 .00 30.4 30.4 EqK = 9.88 1 C=120 0.00 0.0 0.0 8 .22 0. 001 14 .00 0.0 30.4 Vel = 0.73 54 .49 2.157 13.00 30.4 30.4 EqK = 9.88 21 C=120 0.00 0.0 0.0 62.72 0.032 13.00 0.4 30.4 Vel = 5.56 54 .84 2. 157 1T 101 .89 30.8 30.8 EqK = 9.88 4 C=120 12.31 0.0 0.0 117.56 0.103 114 .20 11.8 30.8 Vel = 10.42 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 ' 10:48 Tyco Fire Products Page 8 REF "C"• TYPES FTNG'S Pe Pv ******* NOTES ******* POINT Qt Pf/ft TOTAL Pf Pn E3 117.56 42. 6 K = 18 .01 54 .49 1.049 1T 6.50 23.7 23.7 K = 11.20 21S C=120 5.00 -2.8 0.0 54 .49 0.831 11.50 9.6 23.7 Vel = 20.43 21 54 .49 30.4 K = 9.88 54 .84 1.049 1T 6.50 24.0 24 .0 K = 11.20 4S C=120 5.00 -2.8 0.0 54.84 0.841 11.50 9.7 24 .0 Vel = 20.56 4 54 .84 30.8 K = 9.88 PATH 4 FROM HYDRAULIC REFERENCE 2 TO C2 54 .73 1. 049 1T 6.50 23.9 23.9 K = 11.20 2S C=120 5.00 -2.8 0.0 54.73 0.838 11.50 9. 6 23.9 Vel = 20.52 2. 157 13.67 30.7 30.7 EqK = 9.88 2 C=120 0.00 0.0 0.0 44 .69 0.017 13.67 0.2 30.7 Vel = 3.96 54 .92 2. 157 14 .00 30. 9 30.9 EqK = 9.88 19 C=120 0.00 0.0 0.0 99.61 0.076 14 .00 1.1 30.9 Vel = 8.83 2.157 1T 120.17 32.0 32.0 18 C=120 12.31 0.0 0.0 99.61 0.076 132.48 10.0 32.0 Vel = 8.83 6.357 14 .00 42. 0 42.0 Cl C=120 0.00 0.0 0.0 99. 61 0.000 14 .00 0.0 42.0 Vel = 1.02 C2 99.61 42.0 K = 15.36 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:48 Tyco Fire Products Page 9 REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* POINT Qt Pf/ft TOTAL Pf Pn 54 .92 1.049 1T 6.50 24.0 24 .0 K = 11.20 19S C=120 5.00 -2.8 0.0 54 .92 0.843 11.50 9.7 24.0 Vel = 20.59 19 54.92 30.9` K = 9.88 PATH 5 FROM HYDRAULIC REFERENCE 2 TO 104 54 .73 1.049 1T 6.50 23. 9 23.9 K = 11.20 2S C=120 5.00 -2.8 0.0 54 .73 0.838 11.50 9.6 23. 9 Vel = 20.52 2.157 14 .00 30.7 30.7 EqK = 9.88 2 C=120 0.00 0.0 0.0 10.04 0.001 14 .00 0.0 30.7 Vel = 0.89 54.74 2.157 13.00 30.7 30.7 EqK = 9.88 17 C=120 0.00 0.0 0.0 64.78 0.034 13.00 0.4 30.7 Vel = 5.74 104 64 .78 31. 1 K = 11.61 54 .74 1 .049 1T 6.50 23. 9 23.9 K = 11.20 17S C=120 5.00 -2.8 0.0 54 .74 0.838 11.50 9. 6 23.9 Vel = 20.52 17 54 .74 30.7 K = 9.88 PATH 6 FROM HYDRAULIC REFERENCE 3 TO E5 62.74 1.049 1T 6.50 31.4 31.4 K = 11.20 3S C=120 5.00 -2.8 0.0 62.74 1.079 11.50 12.4 31.4 Vel = 23.52 2. 157 1T 142.56 41. 0 41.0 EqK = 9.80 3 C=120 12.31 0. 0 0.0 34 .44 0.011 154 .87 1. 6 41.0 Vel = 3.05 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 10/ 5/12 10:48 Tyco Fire Products Page 10 REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* POINT Qt Pf/ft TOTAL Pf Pn E5 34 .44 42.6 K = 5.28 PATH 7 FROM HYDRAULIC REFERENCE 3 TO C3 62.74 1.049 1T 6.50 31.4 31.4 K = 11.20 3S C=120 5.00 -2.8 0.0 62.74 1.079 11.50 12.4 31.4 Vel = 23.52 2.157 1T 134.16 41.0 41.0 EqK = 9.80 3 C=120 12.31 0.0 0.0 28.30 0.007 146.47 1.1 41.0 Vel = 2.51 C3 28 .30 42.1 K = 4.36 PATH 8 FROM HYDRAULIC REFERENCE C4 TO E6 13.58 2.157 2T 276.73 42.1 42.1 C4 C=120 24 .61 0.0 0.0 See PATH 2 13.58 0.002 301.34 0. 6 42.1 Vel = 1.20 E6 13.58 42.7 K = 2.08 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) 4 C,?�RLA.S PASTA Drawing Date:9-21-12 9/23/12 22:26 HYDRAULIC DESIGN INFORMATION SHEET Job Name: CARLAS PASTA Location: 50 TALBOT LANE SOUTH WINDSOR, CT. 06074 Drawing Date: 9-21-12 Remote Area Number: 3 Contractor: LEGACY FIRE PROTECTION, INC. Telephone:413 589-0672 592 CENTER STREET PO BOX 582 LUDLOW, MA. 01056 Designer: KPL Calculated By:SprinkCAD www.sprinkcad.com 451 N. Cannon Ave. Lansdale, PA 19446 Construction: STEEL JOIST Occupancy:BAKERY Reviewing Authorities:LOCAL FIRE DEPT SYSTEM DESIGN Code:NFPA 13 Hazard:LIGHT System Type:WET Area of Sprinkler Oper. 1500 sq ftI Sprinkler or Nozzle Density (gpm/sq ft) 0.100 1 Make: Area per Sprinkler 225.0 sq ftl Model: PENDENT Hose Allowance Inside 0 gpm I K-Factor: 5. 60 Hose Allowance Outside 100 gpm I Temperature Rating: 155 CALCULATION SUMMARY 11 Flowing Outlets gpm Required: 363.0 psi Required: 53.6 @ Source WATER SUPPLY Water Flow Test I Pump Data Date of Test 7-10-12 I Rated Capacity 0 gpm I Static Pressure 84 .0 psi I Rated Pressure 0.0 psi I Residual Pres 68.0 psi I Elevation 0 1 At a Flow of 1280 gpm ( Make: 1 Elevation 0" 1 Model: i Location: ON SITE Source of Information: CONTRACT DRAWINGS SYSTEM VOLUME 2111 Gallons Notes: a«iux�u�i .tea' pF.C06&/ ����► .�Q�OPVID yFG�j H�•214 ?0 1*. un � t CARLAS PASTA Drawing Date:9-21-12 9123112 22:26 HYDRAULIC CALCULATION DETAILS HYDRAULIC FLOW LOSS QTY DESCRIPTION LENGTH C! ZD gpm psi TOTALS Hydr Ref W Required at Hyd Area 3 263 49.6 psi 1 6" Grvd Alarm Valve 32' 120 6.065 263 0 .1 1 6" Grvd Butterfly Valve Tyco BFV- 11 ' 120 6.065 263 0 .0 1 6" Fingd Back Flow Valve Ames 200 CHART LOSS 263 2 .5 1 8" x 6" Fingd 90 Ell CI 18' 120 8. 071 263 0.0 Elevation Change 310" 1.3 1 Pipe 8" DIx18 America DI 350 100' 140 8.488 263 0.0 2 8" MJ 90 Ell DI 48' 120 8.071 263 0.0 1 8" Fingd Gate Valve Kennedy Gate 8' 120 8.071 263 0.0 1 8" MJ Tee DI 24' 120 8. 071 263 0.0 Fixed Flow Flow Loss 100 gpm Hydr Ref R1 Required at Source 363 53.6 psi Water Source 84.0 psi static, 68.0 psi residual @ 1280 gpm 363 gpm 82.4 psi SAFETY PRESSURE 28.8 psi Available Pressure of 82.4 psi Exceeds Required Pressure of 53.6 psi This is a safety margin of 28.8 psi or 35 % of Supply Maximum Water Velocity is 21.4 fps CARLAS PASTA Drawing Date:9-21-12 . 9123112 22:26 Page 3 FITTING NAME TABLE ABBREV. NAME C Coupling E 90 ' Standard Elbow F 45' Elbow S Straight Flow Thru Tee T 90 ' Flow Thru Tee V Valve LEGEND HYD REF Hydraulic reference. Refer to accompanying flow diagram. _ K FACTOR Flow factor for open head or path where Flow (gpm) = K x -\/P Qa Flow added or subtracted Qt Total flow DIA Actual internal diameter of pipe C Hazen Williams pipe roughness factor Pf/ft Friction loss per foot of pipe PIPE Length of pipe FTNG'S Number of fittings. See table above. TOTAL Total length (PIPE + FTNG'S) Pt Total pressure (psi) at fitting Pe Pressure due to change in elevation where Pe = 0.433 x change in elevation Pf Friction loss (psi) to fitting where Pf = 1 x 4.52 x (Q/C) ^1.85 / ID^4.87 Pv Velocity pressure (psi) where Pv = 0.001123 x Q^2/ID^4 Pn Normal pressure (psi) , where Pn = Pt - Pv NOTES: - Pressures are balanced to 0.01 psi. Pressures are listed to 0.1 psi. Addition may vary by 0 .1 psi due to accumulation of round off. - Calculations conform to NFPA 13. - Velocity Pressures are not considered in these Calculations t CARLAS PASTA Drawing Date:9-21-12 9123112 22:26 Page 4 NODE ELEVATION SPRINKLER PRESSURE ACTUAL MINIMUM ACTUAL NUMBER K-FACTO .W FLOW DENSITY (FT) (GPM/ (PSI^',�) ) (PSI) (GPM) (GPM) (GPM/SQ.FT) 1 29.50 37.7 2 29.50 37 .7 3 29.50 37.8 4 29.50 37.7 17 29.50 37.7 18 29.50 37.7 19 29.50 37.7 21 29.50 37.7 22 29.50 37.7 23 29.50 37.7 25 29.50 15.3 25S 26.00 5. 60 15.9 22 .3 19. 6 0.11 26 29.50 16.0 26S 26.00 5. 60 16.7 22 .9 19. 6 0.12 27 29.50 17. 9 27S 26.00 5. 60 18.4 24.0 19. 6 0.12 28 29.50 22.6 28S 26.00 5. 60 22. 9 26. 8 22.5 0.12 29 29.50 10.3 29S 26.00 5. 60 11.2 18 .8 14. 8 0 .16 30 29.50 11 .4 30S 26. 00 5. 60 12.2 19. 6 19. 6 0.10 31 29.50 13.1 31S 26.00 5. 60 13.8 20 .8 18.0 0.12 32 29.50 16.0 32S 26.00 5. 60 16. 6 22 . 8 19.5 0 .12 33 29.50 21.8 33S 26.00 5. 60 22.1 26.3 19.5 0.14 34 29.50 21. 6 34S 26.00 5. 60 21.9 26.2 14. 8 0.18 48 29.50 33.7 48S 26.00 5. 60 33.5 32 .4 19.5 0.17 104 29.50 37.7 117 29.50 32. 8 118 29.50 23.8 119 29.50 18.9 120 29.50 17.0 121 29.50 24.1 122 29.50 23.0 123 29.50 16.9 124 29.50 13.8 125 29.50 12.5 126 29.50 35. 6 A9 29.50 37.8 A10 29.50 37.8 All 29.50 37.8 Al2 28.00 38.5 A13 3.00 49.6 Cl 29.50 37. 8 C2 29.50 37. 8 C3 29.50 37.8 { , CARLAS PASTA Drawing Date:9-21-12 9123112 22:26 Page 5 NODE ELEVATION SPRINKLER PRESSURE ACTUAL MINIMUM ACTUAL LOW DENSITY (FT) (GPM/ (PSI-3,z) ) (PSI) (GPM) (GPM) (GPM/SQ.FT) C4 29.50 37.8 El 29.50 37.7 E2 29.50 37.7 E3 29.50 37.7 E4 29.50 37.7 E5 29.50 37.7 E6 29. 50 37.8 Fl 28.00 38.6 W 3. 00 49.6 Max velocity of 21.41 occurs in the pipe from 121 TO E4 Nodes with "S" indicate a node at the top of a sprig or bottom of drop pendent. The node without an "S" is on the branch. 1 CARLAS PASTA Drawing Date:9-21-12 9123112 22:26 Tyco Fire Products Page 6 HYD. Qa DIA. FITTING PIPE Pt Pt REF "C" TYPES FTNG'S Pe py ******* *** FOiNT t Pf ft TOTAL Pf Pn PATH 1 FROM HYDRAULIC REFERENCE 29 TO W (PRIMARY PATH) 18 .77 1.049 1E 3.50 11.2 11.2 K = 5.60 29S C=120 2.00 -1.5 0.0 18.77 0.116 5.50 0 .6 11.2 Vet = 7 .03 1 .049 1E 11 .78 10.3 10.3 EqK = 5.83 29 C=120 1T 7 .00 0.0 0. 0 18.77 0.116 18.78 2 .2 10.3 Vel = 7 .03 19. 60 1 .380 11.57 12 .5 12.5 125 C=120 0.00 0 .0 0. 0 See PATH 2 38.37 0 .114 11 .57 1 .3 12.5 Vel = 8.31 20.82 1.380 12.00 13.8 13. 8 124 C=120 0.00 0 .0 0.0 See PATH 3 59. 19 0.255 12 .00 3.1 13.8 Vel = 12.82 22. 82 1.380 13.00 16.9 16.9 123 C=120 0 .00 0.0 0.0 See PATH 5 82 .01 0.466 13 .00 6.1 16. 9 Vel = 17 .76 26.33 1.610 3.00 23 .0 23.0 122 C=120 0.00 0.0 0.0 See PATH 9 108.33 0.368 3.00 1 .1 23.0 Vel = 17 .24 26.23 1. 610 1T 16. 86 24 .1 24 .1 121 C=120 8.00 0.0 0.0 See PATH 8 134.56 0.549 24 .86 13.7 24.1 Vel = 21.41 88. 14 6.357 12. 63 37.7 37. 7 E4 C=120 0 . 00 0.0 0.0 See PATH 4 222.70 0.002 12. 63 0.0 37.7 Vel = 2 .27 29.46 6.357 14 .00 37.7 37.7 E5 C=120 0.00 0.0 0.0 See PATH 14 AND 11 252.16 0.002 14.00 0.0 37 .7 Vel = 2 .57 -0.83 6.357 2 .71 37 .8 37. 8 E6 C=120 0.00 0 .0 0.0 See PATH 15 251.33 0.002 2 .71 0.0 37. 8 Vel = 2.57 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 9/23/12 22:26 Tyco Fire Products Page 7 HYD. Qa DIA. FITTING PIPE Pt Pt REF "C" TYPES FTNG'S Pe py ******* **** INT Qt Pf/ft TOTAL Pf Pn PATH 1 FROM HYDRAULIC REFERENCE 29 TO W (PRIMARY PATH) 11. 67 6.357 0.46 37 .8 37.8 A10 C=120 0.00 0.0 0.0 See PATH 12 263.00 0 .002 0.46 0.0 37.8 Vel = 2 .68 8 .249 3E 120.52 37.8 37.8 All C=120 60 .05 0. 6 0.0 263.00 0.001 180.57 0.1 37 .8 Vel = 1.59 8.249 1E 43.56 38.5 38.5 A1.2. C=120 20.02 0.0 0. 0 263.00 0.001 63.58 0.0 38.5 Vel = 1 .59 6.357 2E 25.00 38 . 6 38. 6 F1 C=120 35.21 10.8 0.0 263.00 0.002 60.21 0.1 38. 6 Vel = 2 . 68 6.357 2.75 49. 6 49. 6 A13 C=120 0 .00 0 .0 0.0 263.00 0.002 2 .75 0.0 49. 6 Vel = 2.68 W 263.00 49. 6 K = 37 .35 PATH 2 FROM HYDRAULIC REFERENCE 30 TO 125 19.60 1.049 lE 3.50 12.3 12.3 K = 5. 60 30S C=120 2 .00 -1.5 0 . 0 19.60 0.125 5.50 0.7 12.3 Vet = 7.35 1.049 lE 1.78 11 .4 11.4 EqK = 5.80 30 C=120 1T 7.00 0.0 0.0 19. 60 0.125 8.78 1 .1 11.4 Vel = 7 .35 125 19. 60 12.5 K = 5.54 PATH 3 FROM HYDRAULIC REFERENCE 31 TO 124 20.82 1.049 lE 3 .50 13.8 13. 8 K = 5. 60 31S C=120 2 .00 -1 .5 0.0 20.82 0.140 5.50 0.8 13.8 Vet = 7.81 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 9123112 22:26 Tyco Fire Products Page 8 HYD. Qa DIA. FITTING PIPE Pt Pt REF licit TYPES FTNW.13 NOTES ***** * POINT Qt Pf/ft TOTAL Pf Pn PATH 3 FROM HYDRAULIC REFERENCE 31 TO 124 CONTINUED 1 .049 1T 0.45 13.1 13.1 EqK = 5.76 31 C=120 5.00 0.0 0.0 20. 82 0.140 5.45 0 .8 13.1 Vel = 7 .81 124 20.82 13.8 K = 5. 60 PATH 4 FROM HYDRAULIC REFERENCE 25 TO E4 22.35 1.049 1E 3.50 15.9 15. 9 K = 5. 60 25S C=120 2 .00 -1.5 0.0 22 .35 0.160 5.50 0. 9 15. 9 Vel = 8.38 1.049 1E 8.50 15.3 15.3 EqK = 5.72 25 C=120 2 .00 0.0 0.0 22 .35 0.160 10.50 1.7 15.3 Vel = 8 .38 22 .85 1.380 12 .69 17 .0 17.0 120 C=120 0.00 0.0 0. 0 See PATH 6 45.20 0.155 12. 69 2.0 17. 0 Vel = 9.79 24 .04 1.380 14 .43 18 .9 18. 9 119 C=120 0.00 0.0 0.0 See PATH 7 69.25 0.341 14 .43 4.9 18. 9 Vel = 15 .00 26.80 1.380 14 .34 23.8 23. 8 118 C=120 0.00 0.0 0. 0 See PATH 10 96.04 0. 624 14.34 8. 9 23.8 Vel = 20.80 1 .610 1T 8 .71 32.8 32. 8 117 C=120 8 .00 0.0 0.0 96.04 0.294 16.71 4.9 32. 8 Vet = 15.28 -4 .03 6.357 13.12 37 .7 37.7 E2 C=120 0.00 0.0 0. 0 See PATH 12 92 .01 0.000 13.12 0.0 37.7 Vel = 0. 94 -3.87 6.357 1.37 37.7 37.7 E3 C=120 0.00 0.0 0.0 See PATH 13 88.14 0.000 1.37 0.0 37. 7 Vel = 0.90 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 9123112 22:26 Tyco Fire Products Page 9 HYD. Qa DIA. FITTING PIPE Pt Pt REF "C" TYPES FTN ' ******* POINT Qt Pf/ft TOTAL Pf Pn E4 88.14 37.7 K = 14 .35 PATH 5 FROM HYDRAULIC REFERENCE 32 TO 123 22.82 1.049 1E 3.50 16. 6 16. 6 K = 5. 60 32S C=120 2 .00 -1.5 0. 0 22 .82 0.166 5.50 0.9 16. 6 Vel = 8.55 1.049 1T 0.45 16.0 16.0 EqK = 5.71 32 C=120 5.00 0.0 0.0 22.82 0.166 5.45 0. 9 16.0 Vel = 8.55 123 22 . 82 16.9 K = 5.55 PATH 6 FROM HYDRAULIC REFERENCE 26 TO 120 22.85 1.049 1E 3.50 16.7 16.7 K = 5. 60 26S C=120 2.00 -1.5 0.0 22 .85 0.167 5.50 0 .9 16.7 Vel = 8 .57 1.049 1T 0.50 16.0 16.0 EqK = 5 . 70 26 C=120 5.00 0.0 0. 0 22.85 0.167 5.50 0. 9 16.0 Vel = 8.57 120 22.85 17 .0 K = 5.55 PATH 7 FROM HYDRAULIC REFERENCE 27 TO 119 24.04 1 .049 lE 3 .50 18.4 18.4 K = 5. 60 27S C=120 2.00 -1.5 0.0 24.04 0 .183 5.50 1.0 18.4 Vel = 9.01 1. 049 1T 0.50 17 . 9 17. 9 EqK = 5. 68 27 C=120 5.00 0.0 0.0 24 .04 0 .183 5.50 1 .0 17.9 Vel = 9.01 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) I CARLAS PASTA Drawing Date:9-21-1.2 9123112 22:26 Tyco Fire Products Page 10 HYD. Qa DIA. FITTING PIPE Pt Pt REF "C" TYPES FTNGIS pe P-N7 ******* NOTE2 ***** POINT Qt Pf/ft TOTAL Pf Pn 119 24 .04 18 .9 K = 5.53 PATH 8 FROM HYDRAULIC REFERENCE 34 TO 121 26.23 1.049 1E 3.50 21.9 21. 9 K = 5. 60 34S C=120 2 .00 -1 .5 0.0 26.23 0.215 5.50 1 .2 21. 9 Vel = 9. 83 1 .049 1T 6.45 21 .6 21. 6 EqK = 5.64 34 C=120 5.00 0.0 0.0 26.23 0.215 11.45 2 .5 21. 6 Vel = 9.83 121 26.23 24 .1 K = 5.35 PATH 9 FROM HYDRAULIC REFERENCE 33 TO 122 26.33 1.049 1E 3 .50 22 .1 22.1 K = 5. 60 33S C=120 2 .00 -1 .5 0. 0 26.33 0.216 5.50 1 .2 22.1 Vel = 9.87 1.049 1T 0 .45 21 .8 21.8 EqK = 5. 64 33 C=120 5.00 0.0 0. 0 26.33 0 .216 5 .45 1 .2 21. 8 Vel = 9.87 122 26.33 23.0 K = 5.50 PATH 10 FROM HYDRAULIC REFERENCE 28 TO 118 26.80 1.049 1E 3.50 22 . 9 22. 9 K = 5.60 28S C=120 2 .00 -1 .5 0. 0 26.80 0.224 5.50 1 .2 22. 9 Vel = 10.05 1.049 1T 0.50 22 . 6 22. 6 EqK = 5. 64 28 C=120 5 .00 0.0 0. 0 26.80 0 .224 5.50 1 .2 22. 6 Vel = 10.05 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 9123112 22:26 Tyco Fire Products Page 11 HYD. Qa DIA. FITTING PIPE Pt Pt REF licit TYPES FTNG'S Pe Pv ******* NOTES ******* POINT Qt Pf/ft TOTAL Pf Pn 118 26.80 23.8 K = 5.49 PATH 11 FROM HYDRAULIC REFERENCE 48 TO E5 32.40 1 .049 lE 3.50 33.5 33.5 K = 5. 60 48S C=120 2 .00 -1.5 0. 0 32.40 0.318 5.50 1 .7 33.5 Vel = 12 .14 1 .049 1T 0 . 91 33.7 33.7 EqK = 5 .58 48 C=120 5.00 0.0 0.0 32.40 0.318 5 . 91 1 . 9 33. 7 Vel = 12 .14 1.380 1T 19.86 35.6 35. 6 126 C=120 6.00 0.0 0.0 32.40 0.084 25. 86 2.2 35. 6 Vel = 7 .02 E5 32 .40 37 .7 K = 5.27 PATH 12 FROM HYDRAULIC REFERENCE E2 TO A10 4.03 6.357 0 .88 37 .7 37.7 E2 C=120 0.00 0.0 0.0 See PATH 4 4 .03 0.000 0.88 0 .0 37.7 Vel = 0 .04 2.157 1T 101.89 37 .7 37. 7 El C=120 12 .31 0.0 0. 0 4 .03 0.000 114 .20 0 .0 37 .7 Vel = 0.36 2. 157 13.00 37.7 37.7 104 C=120 0.00 0.0 0.0 4 .03 0.000 13.00 0.0 37.7 Vel = 0 .36 2.157 14 .00 37.7 37.7 17 C=120 0.00 0 .0 0.0 4.03 0.000 14 ..00 0 .0 37.7 Vel = 0.36 2.157 13. 67 37 .7 37.7 2 C=120 0.00 0.0 0.0 4.03 0.000 13.67 0 .0 37.7 Vel = 0.36 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 9123112 22:26 Tyco Fire Products Page 12 HYD. 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FITTING PIPE Pt Pt REF licit TYPES FTNGIS p e, P-,r *** ** ****** POINT Qt Pf/ft TOTAL Pf Pn PATH 12 FROM HYDRAULIC REFERENCE E2 TO A10 CONTINUED 2.157 14 .00 37 .7 37.7 19 C=120 0 .00 0.0 0.0 4 .03 0.000 14 .00 0.0 37.7 Vel = 0.36 2 .157 1T 120.17 37.7 37.7 18 C=120 12.31 0.0 0.0 4.03 0 .000 132 .48 0.0 37.7 Vel = 0.36 6.357 14 .00 37.8 37. 8 Cl C=120 0 .00 0.0 0.0 4.03 0 .000 14.00 0.0 37.8 Vel = 0 .04 3. 87 6.357 14 .00 37.8 37. 8 C2 C=120 0.00 0.0 0.0 See PATH 13 7.90 0.000 14 .00 0.0 37.8 Vel = 0.08 2.94 6.357 14 .00 37 .8 37.8 C3 C=120 0.00 0.0 0.0 See PATH 14 10.84 0 .000 14 .00 0.0 37.8 Vel = 0 . 11 0.83 6.357 1T 2 .71 37.8 37.8 C4 C=120 37 .72 0.0 0.0 See PATH 15 11.67 0.000 40.43 0.0 37.8 Vel = 0.12 6.357 1T 276.73 37 .8 37.8 A9 C=120 37 .72 0.0 0.0 11.67 0 .000 314 .45 0.0 37.8 Vel = 0 . 12 A10 11.67 37 .8 K = 1 . 90 PATH 13 FROM HYDRAULIC REFERENCE E3 TO C2 3.87 2 .157 1T 101 .89 37.7 37.7 E3 C=120 12.31 0.0 0.0 See PATH 4 3.87 0.000 114 .20 0.0 37.7 Vel = 0.34 2 .157 13 .00 37.7 37.7 4 C=120 0 .00 0 .0 0.0 3.87 0.000 13. 00 0.0 37.7 Vel = 0.34 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 9123112 22:26 Tyco Fire Products Page 13 HYD. 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FITTING PIPE Pt Pt REF licit TYPE ' ** r** NOTES ******* POINT Qt Pf/ft TOTAL Pf Pn PATH 13 FROM HYDRAULIC REFERENCE E3 TO C2 CONTINUED 2 .157 14.00 37.7 37.7 21 C=120 0.00 0.0 0.0 3. 87 0.000 14 .00 0.0 37 .7 Vel = 0 .34 2.157 13. 67 37 .7 37.7 1 C=120 0. 00 0.0 0.0 3 .87 0.000 13.67 0.0 37.7 Vel = 0 .34 2 .157 14 .00 37 .7 37 .7 23 C=120 0.00 0.0 0.0 3.87 0.000 14 .00 0.0 37.7 Vel = 0.34 2 .157 1T 120.17 37.7 37.7 22 C=120 12.31 0 .0 0.0 3. 87 0.000 132.48 0.0 37.7 Vel = 0 .34 C2 3.87 37 .8 K = 0. 63 PATH 14 FROM HYDRAULIC REFERENCE E5 TO C3 2 . 94 2 .157 1T 142.56 37 .7 37.7 E5 C=120 12.31 0.0 0.0 See PATH 1 AND 11 2. 94 0.000 154 .87 0.0 37.7 Vel = 0 .26 2.157 IT 134 .16 37.8 37.8 3 C=120 12.31 0.0 0.0 2. 94 0.000 146.47 0.0 37. 8 Vel = 0.26 C3 2.94 37.8 K = 0 .48 PATH 15 FROM HYDRAULIC REFERENCE E6 TO C4 0.83 2.157 2T 276.73 37 .8 37. 8 E6 C=120 24 . 61 0.0 0.0 See PATH 1 0.83 0 .000 301.34 0.0 37. 8 Vel = 0 .07 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) l CARLAS PASTA Drawing Date:9-21-12 9123112 22:26 Tyco Fire Products Page 14 HYD. Qa DIA. FITTING PIPE Pt Pt REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* POINT Qt Pf/ft TOTAL Pf Pn C4 0.83 37.8 K = 0 .14 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) Job Water Required Hose Allowance CARLAS PASTA Static Pres: 84.0 psi Pressure: 53.6 psi In: 0 gpm - 50 TALBOT LANE Resid. Pres: 68.0 psi Sys Flow: 263 gpm Out: 100 gpm SOUTH WINDSOR, CT. 06074 Flow: 1280 gpm Sys+Hose: 363 gpm Remote Area: 3 Date: 7-10-12 Safety Pres: 28.8 psi Loc: ON SITE Hd Elv Pres: 10.0 psi 140 12Q 100 Su I 80 P S I 60 100 gpm hose 40 20 10.0 psi 100 150 200 250 300 360 400 450 500 Flaw(anml CARLAS PASTA Drawing Date:9-21-12 9123112 22:27 HYDRAULIC DESIGN INFORbMTION SHEET Job Name: CARLAS PASTA Location: 50 TALBOT LANE SOUTH WINDSOR, CT. 06074 Drawing Date: 9-21-12 Remote Area Number: 4 Contractor: LEGACY FIRE PROTECTION, INC. Telephone:413 589-0672 592 CENTER STREET PO BOX 582 LUDLOW, MA. 01056 Designer: KPL Calculated By:SprinkCAD www.sprinkcad.com 451 N. Cannon Ave. Lansdale, PA 19446 Construction: STEEL JOIST Occupancy:BAKERY Reviewing Authorities:LOCAL FIRE DEPT SYSTEM DESIGN Code:NFPA 13 Hazard:LIGHT System Type:WET Area of Sprinkler Oper. 1500 sq ftj Sprinkler or Nozzle Density (gpm/sq ft) 0.100 1 Make: Area per Sprinkler 330.0 sq ftj Model: PENDENT Hose Allowance Inside 0 gpm I K-Factor: 5.60 Hose Allowance Outside 100 gpm I Temperature Rating: 155 CALCULATION SUMMARY 16 Flowing Outlets gpm Required: 383.9 psi Required: 37.4 @ Source WATER SUPPLY Water Flow Test ( Pump Data Date of Test 7-10-12 Rated Capacity 0 gpm Static Pressure 84.0 psi Rated Pressure 0.0 psi Residual Pres 68.0 psi Elevation 0 At a Flow of 1280 gpm Make: Elevation 0" Model: Location: ON SITE Source of Information: CONTRACT DRAWINGS SYSTEM VOLUME 2111 Gallons Notes: "OWN' CF c11r NA � a p * o *g No.21484 * Q AaO NAI N6 r �D„ CARLAS PASTA Drawing Date:9-21-12 9/23/12 22:27 HYDRAULIC CALCULATION DETAILS HYDRAULIC FLOW LOSS QTY DESCRIPTION LENGTH C Hydr Ref W Required at Hyd Area 4 284 33.6 psi 1 6" Grvd Alarm Valve 32' 120 6.065 284 0.1 1 6" Grvd Butterfly Valve Tyco BFV- 11' 120 6.065 284 0.0 1 6" Fingd Back Flow Valve Ames 200 CHART LOSS 284 2.2 1 8" x 6" Fingd 90 Ell CI 18' 120 8.071 284 0.0 Elevation Change 3101' 1.3 1 Pipe 8" DIx18 America DI 350 100' 140 8.488 284 0.1 2 8" MJ 90 Ell DI 48' 120 8.071 284 0.0 1 8" Fingd Gate Valve Kennedy Gate 8' 120 8.071 284 0.0 1 8" MJ Tee DI 24' 120 8.071 284 0.0 Fixed Flow Flow Loss 100 gpm Hydr Ref R1 Required at Source 384 37.4 psi Water Source 84.0 psi static, 68.0 psi residual @ 1280 gpm 384 gpm 82.3 psi SAFETY PRESSURE 44.9 psi Available Pressure of 82.3 psi Exceeds Required Pressure of 37.4 psi. This is a safety margin of 44.9 psi or 55 % of Supply Maximum Water Velocity is 13.7 fps CARLAS PASTA Drawing Date:9-21-12 9/23/12 22:27 Page 3 FITTING NAME TABLE ABBREV. NAME C Coupling E 90 ' Standard Elbow F 45' Elbow S Straight Flow Thru Tee T 90' Flow Thru Tee V Valve LEGEND HXD REF Hydraulic reference. Refer to accompanying flow diagram. K FACTOR Flow factor for open head or path where Flow (gpm) = K x -\/P Qa Flow added or subtracted Qt Total flow DIA Actual internal diameter of pipe C Hazen Williams pipe roughness factor Pf/ft Friction loss per foot of pipe PIPE Length of pipe FTNG'S Number of fittings. See table above. TOTAL Total length (PIPE + FTNG'S) Pt Total pressure (psi) at fitting Pe Pressure due to change in elevation where Pe = 0.433 x change in elevation Pf Friction loss (psi) to fitting where Pf = 1 x 4.52 x (Q/C) ^1.85 / ID^4 . 87 Pv Velocity pressure (psi) where Pv = 0.001123 x Q^2/ID^4 Pn Normal pressure (psi) , where Pn = Pt - Pv NOTES: - Pressures are balanced to 0.01 psi. Pressures are listed to 0.1 psi. Addition may vary by 0.1 psi due to accumulation of round off. - Calculations conform to NFPA 13. - Velocity Pressures are not considered in these Calculations CARLAS PASTA Drawing Date:9-21-12 9/23/12 22:27 Page 4 NODE ELEVATION SPRINKLER PRESSURE ACTUAL MINIMUM ACTUAL NUMBER K--FACTOR FLOW FL OW MNSITY (PSI) (GPM) (GPM) (GP K/SQ.FT) 1 29.50 21.9 2 29.50 21. 9 3 29.50 21.9 .4 29.50 21. 9 17 29.50 21. 9 18 29.50 21.9 19 29.50 21 .9 21 29.50 21.9 22 29.50 21.9 23 29.50 21. 9 36 10. 67 8.2 36S 10.00 5. 60 8.2 16.1 15.6 0.10 37 10. 67 8. 9 37S 10 .00 5. 60 9.0 16.8 15. 6 0.11 38 10. 67 8 .2 38S 10.00 5. 60 8.3 16.1 15.6 0.10 39 10. 67 9.0 39S 10.00 5. 60 9.0 16.8 15. 6 0.11 40 10. 67 0.2 40S 10.00 5. 60 9.2 17 .0 14.8 0 .11 41 10. 67 9.4 41S 10.00 5. 60 9.4 17.2 14.8 0.12 42 10. 67 9. 6 42S 10.00 5. 60 9.7 17.4 14 .8 0.12 43 10. 67 9. 9 43S 10.00 5. 60 9. 9 17 .6 14.8 0.12 44 10. 67 7.1 44S 10.00 5. 60 7.1 15.0 14 .8 0.10 45 10. 67 7.4 45S 10.00 5. 60 7.5 15.3 14 . 8 0.10 46 10. 67 7.8 46S 10.00 5. 60 7.8 15.7 14. 8 0.11 47 10. 67 9.3 47S 10.00 11.20 8.7 33.0 33.0 0.10 49 10. 67 10.1 49S 10.00 5. 60 10.1 17.8 15. 6 0.11 50 10. 67 9.4 50S 10.00 5. 60 9.4 17.2 15.6 0.11 51 10. 67 9. 8 51S 10.00 5.60 9.8 17.6 14.8 0.12 52 10. 67 9.8 52S 10.00 5.60 9.8 17.5 14 .8 0.12 104 29.50 21. 9 105 10. 67 10.4 106 10. 67 9.4 107 10. 67 9. 9 108 10. 67 9.8 109 10. 67 10.4 110 10. 67 9.5 111 10. 67 9. 9 112 10. 67 8.3 CARLAS PASTA Drawing Date:9-21-12 9123112 22:27 Page 5 NODE ELEVATION SPRINKLER PRESSURE ACTUAL MINIMUM ACTUAL NUMBER K-FACTOR FLOW FLOW DENSITY PSI) (GPM) (GPM) (GPM/SQ.FT) 113 10.67 7. 9 114 10. 67 10.7 115 10.67 10.4 116 10. 67 11.2 A9 29.50 21.9 A10 29.50 21.9 All 29.50 21. 9 Al2 28.00 22.5 A13 3.00 33.6 Cl 29.50 21 . 9 C2 29.50 21. 9 C3 29.50 21. 9 C4 29.50 21. 9 D1 10 .67 11 .7 D2 10. 67 11.8 D3 10.67 11. 9 D4 10. 67 12.5 El 29.50 21.9 E2 29.50 21.9 E3 29.50 21.9 E4 29.50 21. 9 E5 29.50 21. 9 E6 29.50 21. 9 F1 28.00 22.6 W 3.00 33. 6 Max velocity of 13. 68 occurs in the pipe from ill TO D3 Nodes with "S" indicate a node at the top of a sprig or bottom of drop pendent. The node without an "S" is on the branch. CARLAS FASTA Drawing Date:9-21-12 9123112 22:27 Tyco Fire Products Page 6 HYD. Qa DIA. FITTING PIPE Pt Pt REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* TOTAL Pf Pn PATH 1 FROM HYDRAULIC REFERENCE 44 TO W (PRIMARY PATH) 14. 96 1.049 lE 0.67 7.1 7.1 K = 5. 60 44S C=120 2.00 -0.3 0.0 14. 96 0. 076 2. 67 0.2 7.1 Vel = 5. 61 1.049 1E 9.14 7.1 7.1 EqK = 5. 63 44 C=120 2.00 0.0 0.0 14. 96 0.076 11.14 0.8 7.1 Vel = 5. 61 15.32 1.380 5.04 7.9 7.9 113 C=120 0.00 0.0 0.0 See PATH 2 30. 29 0.074 5.04 0.4 7.9 Vel = 6.56 15. 67 1.380 10.51 8.3 8.3 112 C=120 0.00 0.0 0.0 See PATH 3 45.96 0.160 10.51 1.7 8.3 Vel = 9. 95 17.18 1.380 1T 0.95 9.9 9.9 ill C=120 6.00 0.0 0.0 See PATH 11 63.13 0.287 6.95 2.0 9.9 Vel = 13. 68 187 .76 3.260 9.24 11.9 11.9 D3 C=120 0.00 0.0 0.0 See PATH 4 AND 15 250. 90 0.056 9.24 0.5 11.9 Vel = 9.74 33.00 3.260 4E 192 .19 12.5 12.5 D4 C=120 1T 57.79 -7.5 0.0 See PATH 9 283. 90 0.070 249.98 17. 6 12.5 Vel = 11 .02 8.249 1E 43.56 22.5 22.5 Al2 C=120 20.02 0.0 0.0 283.90 0.001 63.58 0.0 22.5 Vel = 1.72 6.357 2E 25.00 22. 6 22. 6 F1 C=120 35.21 10.8 0.0 283. 90 0.003 60.21 0.2 22. 6 Vel = 2.90 6.357 2.75 33.6 33. 6 A13 C=120 0.00 0.0 0.0 283.90 0.003 2.75 0.0 33. 6 Vel = 2.90 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 9/23/12 22:27 Tyco Fire Products Page 7 HYD. 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FITTING PIPE Pt Pt REF "`C" TYPES FTNG'S Pe Pv ******* NOT ******* Pf Pn W 283.90 33.6 K = 48.97 PATH 2 FROM HYDRAULIC REFERENCE 45 TO 113 15.32 1.049 lE 0.67 7.5 7.5 K = 5.60 45S C=120 2.00 -0.3 0.0 15.32 0 .080 2.67 0.2 7.5 Vel = 5.74 1.049 1T 1.14 7.4 7.4 EqK = 5.63 45 C=120 5.00 0.0 0.0 15.32 0.080 6.14 0.5 7.4 Vel = 5.74 113 15.32 7.9 K = 5.45 PATH 3 FROM HYDRAULIC REFERENCE 46 TO 112 15.67 1.049 lE 0. 67 7.8 7.8 K = 5. 60 46S C=120 2.00 -0.3 0.0 15.67 0.083 2 . 67 0.2 7.8 Vel = 5.87 1.049 1T 1.14 7.8 7.8 EqK = 5. 62 46 C=120 5.00 0.0 0.0 q 15.67 0.083 6.14 0.5 7 . 8 Vel = 5.87 112 15. 67 8.3 K = 5.45 PATH 4 FROM HYDRAULIC REFERENCE 36 TO D3 16.07 1.049 lE 0. 67 8.2 8.2 K = 5. 60 36S C=120 2.00 -0.3 0.0 16.07 0.087 2.67 0.2 8.2 Vel = 6.03 1.049 lE 12.50 8.2 8.2 EqK = 5.62 36 C=120 2 .00 0.0 0.0 16.07 0.087 14 .50 1.3 8.2 Vel = 6.03 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARL, S PASTA Drawing Date:9-21-12 9123112 22:27 ` Tyco Fire Products Page 8 HYD. 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FITTING PIPE Pt Pt REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* TOTAL Pf Pn PATH 4 FROM HYDRAULIC REFERENCE 36 TO D3 CONTINUED 16.77 1.380 11.00 9.4 9.4 106 C=120 0.00 0.0 0.0 See PATH 6 32.84 0.086 11.00 0.9 9.4 Vel = 7.11 17.52 1.380 1T 0.95 10.4 10.4 105 C=120 6.00 0.0 0.0 See PATH 13 50.36 0.189 6.95 1.3 10.4 Vel = 10.91 34.14 3.260 8.00 11.7 11.7 Dl C=120 0.00 0.0 0.0 See PATH 8 84.50 0.007 8.00 0.1 11.7 Vel = 3.28 67.90 3.260 8.25 11.8 11.8 D2 C=120 0.00 0.0 0.0 See PATH 5 AND 12 152.40 0.022 8.25 0.2 11.8 Vel = 5.92 D3 152.40 11.9 K = 44 .11 PATH 5 FROM HYDRAULIC REFERENCE 38 TO D2 16.12 1.049 lE 0.67 8.3 8.3 K = 5. 60 38S C=120 2.00 -0.3 060 16.12 0.087 2. 67 0.2 8.3 Vel = 6.04 1.049 1E 12.50 8.2 8.2 EqK = 5. 62 38 C=120 2 .00 0.0 0. 0 16.12 0.087 14 .50 1.3 8.2 Vel = 6.04 16.81 1 .380 11.00 9.5 9.5 110 C=120 0.00 0.0 0.0 See PATH 7 32 .92 0.086 11.00 0. 9 9.5 Vel = 7.13 17.57 1.380 1T 0.95 10.4 10.4 109 C=120 6.00 0.0 0.0 See PATH 14 50.49 0.190 6. 95 1.3 10.4 Vel = 10.94 D2 50.49 11.8 K = 14 .73 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 9/23/12 22:27 Tyco Fire Products Page 9 HYD. Qa DIA. FITTING PIPE Pt Pt REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* TOTAL Pf Pn PATS 6 FROM HYDRAULIC REFERENCE 37 TO 106 16.77 1.049 lE 0.67 9.0 9.0 K - 5. 60 37S C=120 2.00 -0.3 0.0 16.77 0.094 2.67 0.2 9.0 Vel = 6.28 1.049 1T _ 0.50 8.9 8. 9 EqK - 5.61 37 C=120 5.00 0.0 0.0 16.77 0.094 5.50 0.5 8.9 Vel = 6.28 106 16.77 9.4 K = 5.46 PATS 7 FROM HYDRAULIC REFERENCE 39 TO 110 16.81 1.049 lE 0. 67 9.0 9.0 K = 5. 60 39S C=120 2.00 -0.3 0.0 16.81 0.094 2.67 0.3 9.0 Vel = 6.30 1.049 1T 0.50 9.0 9.0 EqK = 5.61 39 C=120 5.00 0.0 0.0 16.81 0.094 5.50 0.5 9.0 Vel = 6.30 110 16.81 9.5 K = 5.46 PATH 8 FROM HYDRAULIC REFERENCE 40 TO D1 16. 99 1.049 lE 0. 67 9.2 9.2 K = 5.60 40S C=120 2.00 -0.3 0.0 16. 99 0.096 2.67 0.3 9.2 Vel = 6.37 1.049 1T 1.75 9.2 9.2 EqK = 5.61 40 C=120 5.00 0.0 0.0 16. 99 0.096 6.75 0. 6 9.2 Vel = 6.37 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 9123112 22:27 Tyco Fire Products Page 10 HYD. Qa DIA. FITTING PIPE Pt Pt REF licit TYPES FTNG'S Pe PyNOTES **** Pf7ft TOTAL Pf Pn PATH-8 FROM HYDRAULIC REFERENCE 40 TO Dl CONTINUED 1.380 4 . 97 9.8 9.8 108 C=120 0.00 0.0 0.0 16.99 0.025 4 . 97 0.1 9.8 Vel = 3. 68 17.15 1.380 1T 13.05 9.9 9. 9 107 C=120 6.00 0.0 0.0 See PAT H 10 34.14 0.092 19.05 1.8 9. 9 Vet = 7.39 D1 34.14 11.7 K = 9. 98 PATH 9 FROM HYDRAULIC REFERENCE 47 TO D4 33.00 1.049 lE 0. 67 8.7 8.7 K = 11.20 47S C=120 2.00 -0.3 0.0 33.00 0.329 2.67 0.9 8.7 Vel = 12.37. 1.049 1T 1.00 9.3 9.3 EqK = 10.84 47 C=120 5.00 0.0 0.0 33.00 0.329 6.00 2.0 9.3 Vel = 12.37 1.380 1T 8.08 11.2 11.2 116 C=120 6.00 0.0 0.0 33.00 0.086 14.08 1 .2 11.2 Vel = 7.15 D4 33.00 12.5 K = 9.35 PATH 10 FROM HYDRAULIC REFERENCE 41 TO 107 17.15 1.049 lE 0. 67 9.4 9.4 K = 5. 60 41S C=120 2.00 -0.3 0.0 17 .15 0.098 2. 67 0.3 9.4 Vel = 6.43 1.049 1T 1.02 9.4 9.4 EqK = 5.61 41 C=120 5.00 0.0 0.0 17 .15 0.098 6.02 0.6 9.4 Vel = 6.43 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 9123112 22:27 Tyco Fire Products Page 11 HYD. Qa DIA. FITTING PIPE Pt Pt REF "C" TYPES FTNG'S Pe Pv ******* NOTES ****** TOTAL Pf Pn 107 17.15 9.9 K = 5.44 PATH 11 FROM HYDRAULIC REFERENCE 50 TO 111 17.18 1.049 lE 0. 67 9.4 9.4 K = 5.60 50S C=120 2.00 -0.3 0.0 17.18 0.098 2.67 0.3 9.4 Vel = 6.44 1.049 1T 0.75 9.4 9.4 EqK = 5.61 50 C=120 5.00 0.0 0.0 17.18 0.098 5.75 0.6 9.4 Vel = 6.44 111 17.18 9.9 K = 5.45 PATH 12 FROM HYDRAULIC REFERENCE 42 TO D2 17 .41 1.049 lE 0.67 9.7 9.7 K = 5.60 42S C=120 2.00 -0.3 0.0 17 .41 0.101 2 . 67 0.3 9.7 Vel = 6.53 1.049 1E 13.93 9.6 9. 6 EqK = 5. 61 42 C=120 1T 7.00 0.0 0.0 17 .41 0.101 20.93 2.1 9. 6 Vel = 6.53 D2 17.41 11.8 K = 5.06 PATH 13 FROM HYDRAULIC REFERENCE 52 TO 105 17.52 1.049 1E 0.67 9.8 9.8 K = 5. 60 52S C=120 2.00 -0.3 0.0 17 .52 0.102 2. 67 0.3 9. 8 Vel = 6.57 1.049 1T 1.00 9.8 9.8 EqK = 5.61 52 C=120 5.00 0.0 0.0 17.52 0.102 6.00 0.6 9.8 Vet = 6.57 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 9123112 22:27 Tyco Fire Products Page 12 HYD. Qa DIA. FITTING PIPE Pt Pt REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* TOTAL Pf Pn 105 17.52 10.4 K = 5.44 PATH 14 FROM HYDRAULIC REFERENCE 51 TO 109 17.57 1.049 lE 0.67 9.8 9. 8 K = 5. 60 51S C=120 2 .00 -0.3 0.0 17.57 0.102 2. 67 0.3 9.8 Vel = 6.58 1.049 1T 1.00 9.8 9.8 EqK = 5.60 51 C=120 5.00 0.0 0.0 17.57 0.102 6.00 0. 6 9.8 Vel = 6.58 109 17.57 10.4 K = 5.44 PATH 15 FROM HYDRAULIC REFERENCE 43 TO D3 17 .59 1.049 1E 0.67 9.9 9.9 K = 5.60 43S C=120 2 .00 -0.3 0.0 17.59 0.103 2. 67 0.3 9.9 Vel = 6.59 1.049 IT 0.50 9.9 9. 9 EqK = 5.60 43 C=120 5.00 0.0 0.0 17 .59 0.103 5.50 0. 6 9.9 Vel = 6.59 1.380 8.96 10.4 10.4 115 C=120 0 .00 0.0 0.0 17 .59 0.027 8. 96 0.2 10.4 Vel = 3.81 17.77 1.380 IT 7.05 10.7 10.7 114 C=120 6.00 0.0 0.0 See PATH 16 35.36 0.098 13.05 1.3 10.7 Vel = 7.66 D3 35.36 11. 9 K = 10.23 PATH 16 FROM HYDRAULIC REFERENCE 49 TO 114 17.77 1.049 lE 0.67 10.1 10.1 K = 5. 60 49S C=120 2 .00 -0.3 0.0 17.77 0.105 2. 67 0.3 10.1 Vel = 6.66 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) Job Water Required Hose Allowance CARLAS PASTA Static Pres: 84.0 psi Pressure: 37.4 psi In: 0 gpm 50 TALBOT LANE Resid. Pres: 68.0 psi Sys Flow: 284 gpm Out: 100 gpm SOUTH WINDSOR, CT.06074 Flow: 1280 gpm Sys+Hose: 384 gpm Remote Area:4 Date: 7-10-12 Safety Pres: 44.9 psi 140 Loc: ON SITE Hd Eiv Pres: 3.0 psi 120 100 — Supply 80 P S 1 .60 40 100 gpm hose 20 3.0 psi 100 150 200 250 300 350 400 450 500 Flow(aDml CARLAS PASTA Drawing Date:9-21-12 9123112 22:28 HYDRAULIC DESIGN INFORMATION SHEET Job Name: CARLAS PASTA Location: 50 TALBOT LANE SOUTH WINDSOR, CT. 06074 Drawing Date: 9-21-12 Remote Area Number: 5 Contractor: LEGACY FIRE PROTECTION, INC. Telephone:413 589-0672 592 CENTER STREET PO BOX 582 LUDLOW, MA. 01056 Designer: KPL Calculated By:SprinkCAD www.sprinkcad.com 451 N. Cannon Ave. Lansdale, PA 19446 Construction: STEEL JOIST Occupancy:BAKERY Reviewing Authorities:LOCAL FIRE DEPT SYSTEM DESIGN Code:NFPA 13 Hazard:CLASS 1 System Type: DRY Area of Sprinkler Oper. 2600 sq ftl Sprinkler or Nozzle Density (gpm/sq ft) 0.250 I Make: Area per Sprinkler 120.0 sq ftl Model: UP T Hose Allowance Inside 0 gpm I K-Factor• 8.00 Hose Allowance Outside 500 gpm I Temperatuing: 155 CALCULATION SUMMARY 41 Flowing Outlets gpm Required: 1499.8 psi Required: 52.4 @ Source WATER SUPPLY Water Flow Test I Pump Data Date of Test 7-10-12 I Rated Capacity 0 gpm Static Pressure 84 .0 psi ( Rated Pressure 0.0 psi Residual Pres 68.0 psi I Elevation 0 I At a Flow of 1280 gpm I Make: I Elevation 0" I Model: Location: ON SITE Source of Information: CONTRACT DRAWINGS SYSTEM VOLUME 2111 Gallons / Notes: ,%%Wuawupgyq Of C 0 WAVE AlpVID V0A, �y a io Z x'# v ca r %sle 0 -00 0.21484 � , NS i� CARLAS PASTA Drawing Date:9-21-12 9123112 22:28 HYDRAULIC CALCULATION DETAILS HYDRAULIC FLOW LOSS QTY DESCRIPTION LENGTH C Tn gpm psi TOTS Hydr Ref W Required at Hyd Area 5 1000 41.2 psi 1 6" Grvd Pry Valve VIC NXT PREACTI 22 ' 100 6.065 1000 1.1 1 6" Grvd Butterfly Valve Tyco BFV- 11' 120 6.065 1000 0.4 1 6" Fingd Check Valve 32' 120 6.065 1000 1.1 1 6" Grvd Alarm Valve 32' 120 6.065 1000 1.1 1 6" Grvd Butterfly Valve Tyco BFV- 11' 120 6.065 1000 0.4 1 6" Fingd Back Flow Valve Ames 200 CHART LOSS 1000 4.4 1 8" x 6" Fingd 90 Ell CI 16' 120 8.071 1000 0.2 Elevation Change 310" 1.3 1 Pipe 8" DIx18 America DI 350 100' 140 8 .488 1000 0.5 2 8" MJ 90 Ell DI 48' 120 8.071 1000 0.4 1 8" Fingd Gate Valve Kennedy Gate 8' 120 8.071 1000 0.1 1 8" MJ Tee DI 24 ' 120 8.071 1000 0.2 Fixed Flow Flow Loss 500 gpm Hydr Ref R1 Required at Source 1500 52.4 psi Water Source 84 .0 psi static, 68.0 psi residual @ 1280 gpm 1500 gpm 62.5 psi SAFETY PRESSURE WT10.1 psi Available Pressure of 62.5 psi Exceeds Required Pressure of 52.4 psi This is a safety margin of 10.1 psi or 16 % of Supply Maximum Water Velocity is 15.5 fps ICARLAS PASTA Drawing Date:9-21-12 9123112 22:28 Page 3 FITTING NAME TABLE NAME C Coupling E 90' Standard Elbow F 45' Elbow S Straight Flow Thru Tee T 90' Flow Thru Tee V Valve LEGEND HYD REF Hydraulic reference. Refer to accompanying flow diagram. K FACTOR Flow -factor for open head or path where Flaw (gpm) = K x -\/P Qa Flow added or subtracted Q� Total flow DIA Actual internal diame4Cer of pipe C Hazer. Williams pipe roughness factor Pf/ft Friction loss per foot of pipe PIPE Length of pipe FTNG'S Number of fittings. See table above. TOTAL Total :Length (PIPE + FTNG'S) Pt Total pressure (psi) at fitting Pe Pressure due to change in elevation where Pe = 0.433 x change in elevation Pf Friction loss (psi) to fitting where Pf = 1 x 4.52 x (Q/C) ^1.85 / ID^4 . 87 Pv Velocity pressure (psi) where Pv = 0.001123 x Q^2/IDA4 Pn Normal pressure (psi) , where Pn = Pt - Pv NOTES: - Pressures are balanced to 0.01 psi. Pressures are listed to 0.1 psi. Addition may vary by 0.1 psi due to accumulation of round off. - Calculations conform to NFPA 13. - Velocity Pressures are not considered in these Calculations CARLAS PASTA Drawing Date:9-21-12 9123112 22:28 Page 4 NODE ELEVATION SPRINKLER PRESSURE ACTUAL MINIMUM ACTUAL NUMBER K-FACTOR FLOW FLOW DENSITY P I ) ) (PSI) (GPM) (GPM) (GPM/SQ.FT) 1 29.50 23.0 2 29.50 23.0 3 29.50 22.7 4 29.50 23.6 17 29.50 23.3 18 29.50 22.4 19 29.50 22.7 21 29.50 23.3 22 29.50 22.4 23 29.50 22.7 53 37 .00 8.00 8.3 23.0 21.3 0.27 54 37.00 8.00 7.1 21.3 21.3 0.25 55 37.00 8.00 7.1 21.3 21.3 0.25 56 37 .00 8.00 7.2 21.5 21.3 0.25 57 37.00 8. 00 7.3 21.6 21.3 0.25 58 37.00 8.00 7 .1 21.4 21.3 0.25 59 37.00 8.00 7. 1 21 .3 21.3 0.25 60 37.00 8.00 8.2 22.9 21.3 0.27 61 37.00 8.00 7.1 21.3 21.3 0.25 62 37.00 8.00 7.1 21.4 21.3 0.25 63 37.00 8.00 7.3 21.6 21.3 0.25 64 37. 00 8.00 7 .3 21.7 21.3 0.25 65 37.00 8.00 7.2 21.4 21.3 0.25 66 37.00 8.00 7.1 21.4 21.3 0.25 67 37.00 8. 00 7.2 21.5 21.3 0.25 68 37.00 8.00 7.3 21. 6 21 .3 0.25 69 37.00 8.00 7.4 21 .8 21.3 0.26 70 37.00 8.00 7.5 21.9 21.3 0.26 71 37.00 8.00 7.3 21. 6 21.3 0.25 72 37.00 8.00 7.3 21.6 21.3 0.25 73 37.00 8.00 8.0 22 .7 21 .3 0.27 74 37.00 8.00 7.5 21.9 21 .3 0.26 75 37.00 8.00 7. 6 22.0 21.3 0.26 76 37.00 8.00 7.7 22.2 21.3 0.26 77 37.00 8.00 7.8 22.3 21.3 0.26 78 37.00 8.00 7.6 22 .1 21.3 0.26 79 37.00 8.00 7. 6 22.0 21.3 0.26 80 37.00 8.00 8.0 22. 6 21 .3 0.27 81 37.00 8.00 8.1 22.8 21 .3 0.27 82 37.00 8.00 8.1 22.7 21 .3 0.27 83 37.00 8.00 9. 6 24.8 21.3 0.29 84 27.00 8.00 14.4 30.4 30.0 0.25 85 27.00 8.00 14 .4 30.4 30.0 0.25 86 27.00 8.00 14.5 30.5 30.0 0.25 87 27.00 8.00 14.7 30.7 30.0 0.26 88 27.00 8.00 15.1 31.1 30.0 0.26 89 13.00 8.00 16.1 32.1 30.0 0.27 90 13.00 8.00 18.7 34. 6 30.0 0.29 91 13.00 8.00 16. 1 32 .1 30.0 0.27 92 13.00 8.00 18.9 34.8 30.0 0.29 93 13.00 8.00 16.3 32.3 30 .0 0.27 CARLAS PASTA Drawing Date:9-21-12 9123112 22:28 Page 5 NODE ELEVATION SPRINKLER PRESSURE ACTUAL MINIMUM ACTUAL NUMBER K-FACTOR FLOW FLOW DENSITY (GPM (PSI^'4) ) (PSI) (GPM) (GPM) (GPM/SQ.FT) 100 13.00 22.8 101 13.00 18.9 102 13.00 18.7 103 27.00 16.8 104 29.50 23. 6 Al 37.00 7.8 A2 37.00 7. 9 A3 37.00 8.0 A4 37.00 8.3 A5 37.00 8 . 9 A6 37.00 9.7 A7 37. 00 11.7 A8 19.00 20.8 A9 29.50 19.5 A10 29.50 26.0 All 29.50 26.0 Al2 28.00 28.1 A13 3.00 41.1 B1 20.00 20.0 Cl 29.50 19. 6 C2 29.50 19.6 C3 29.50 19.5 C4 29.50 19.5 E1 29.50 26.0 E2 29.50 26.0 E3 29.50 26.0 E4 29.50 26.0 E5 29.50 26.0 E6 29.50 26.0 F1 28.00 28.6 W 3.00 41.2 Max velocity of 15.48 occurs in the pipe from A7 TO A6 CARLAS PASTA Drawing Date:9-21-12 9123112 22:28 Tyco Fire Products Page 6 HYD. Qa DIA. FITTING PIPE Pt Pt REF licit TYPES FTNG'S Pe Pv ******* NOTES ******* POINT t F TOTAL Pf Pn PATH 1 FROM HYDRAULIC REFERENCE 91 TO N (PRIMARY PATH) 32.06 1.. 049 1T 3.50 16.1 16.1 K = 8.00 91 C=120 5.00 0.0 0.0 32 .06 0.312 8.50 2.6 16.1 Vel = 12.02 32.06 2. 635 0.50 18.7 18.7 102 C=120 0.00 0.0 0.0 See PATH 2 64 .12 0.013 0.50 0.0 18.7 Vel = 3.81 34. 61 2.635 7.37 18.7 18.7 K = 8.00 90 C=120 0.00 0.0 0.0 98.73 0.028 7.37 0.2 18.7 Vel = 5-B-T- _ 34 .80 2.635 0.50 18.9 18.9 K = 8.00 92 C=120 0.00 0.0 0.0 133.53 0.049 0.50 0.0 18.9 Vel = 7. 93 32.27 2.635 lE 44 .59 18.9 18. 9 101 C=120 8.24 0.0 0.0 See PATH 3 165.79 0.073 52.83 3.9 18.9 Vet = 9.85 4.260 1T 7.00 22.8 22.8 100 C=120 26.33 -3.0 0.0 165.79 0.007 33.33 0.2 22.8 Vel = 3.77 153.02 6.357 3E 50.81 20.0 20.0 B1 C=120 52.81 0.4 0.0 See PATH 1.5 318.81 0.003 103.62 0.3 20.0 Vel = 3.25 680. 98 6.357 4E 47.06 20.8 20. 8 A8 C=120 70.41 -4.5 0.0 See PATH 4 999.79 0.028 117.47 3.3 20.8 Vel = 10.21 -201 .39 6.357 2T 276.73 19.5 19.5 A9 C=120 75.44 0.0 0 .0 See PATH 16 798.40 0.018 352.17 6.5 19.5 Vel = 8.15 201.39 6.357 0.46 26.0 26.0 A10 C=120 0.00 0.0 0.0 See PATH 16 999.79 0.028 0.46 0.0 26.0 Vel = 10.21 8.249 3E 120.52 26.0 26.0 All C=120 60.05 0.6 0.0 999.79 0.008 180.57 1.4 26.0 Vel = 6.06 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 9123112 22:28 Tyco Fire Products Page 7 HYD. Qa DIA. FITTING PIPE Pt Pt REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* POINT L)t t TOTAL Pf Pn PATH 1 FROM HYDRAULIC REFERENCE 91 TO W (PRIMARY PATH) 8.249 lE 43.56 28.1 28.1 Al2 C=120 20 .02 0.0 0.0 999.79 0.008 63.58 0.5 28.1 Vel = 6.06 6.357 2E 25.00 28.6 28.6 Fl C=120 35.21 10.8 0.0 999.79 0.028 60.21 1.7 28. 6 Vel = 10.21 6.357 2 .75 41.1 41.1 A13 C=120 0.00 0.0 0.0 999.79 0.028 2.75 0.1 41.1 Vel = 10.21 W 999.79 41.2 K = 155.72 PATH 2 FROM HYDRAULIC REFERENCE 89 TO 102 32 .06 1.049 1T 3.50 16.1 16.1 K = 8.00 89 C=120 5.00 0.0 0.0 32 .06 0.312 8.50 2.6 16.1 Vel = 12.02 102 32 .06 18.7 K = 7 .41 PATH 3 FROM HYDRAULIC REFERENCE 93 TO 101 32.27 1.049 1T 3.50 16.3 16.3 K = 8.00 93 C=120 5.00 0.0 0.0 32 .27 0.315 8.50 2 .7 16.3 Vel = 12.10 lc.l 32.27 18. 9 K = 7.41 PATS 4 FROM HYDRAULIC REFERENCE 54 TO A8 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 9123112 22:28 Tyco Fire Products Page 8 HYD. Qa DIA. FITTING PIPE Pt Pt REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* POINT Qt t TOTAL Pf Pn PATS 4 FROM HYDRAULIC REFERENCE 54 TO A8 CONTINUED 21.25 2 .157 9.25 7.1 7.1 K = 8.00 54 C=120 0.00 0.0 0.0 21.25 0.004 9.25 0.0 7.1 Vel = 1.88 21.31 2.157 9.25 7.1 7.1 K = 8. 00 55 C=120 0.00 0.0 0.0 42.56 0.016 9.25 0.1 7. 1 Vel = 3.77 21.53 2.157 1T 5.45 7 .2 7.2 K = 8.00 56 C=120 12.31 0.0 0.0 64.09 0.034 17.75 0.6 7.2 Vel = 5. 68 64.32 4.260 9.17 7.8 7. 8 Al C=120 0.00 0.0 0.0 See PATH 6 128.40 0.004 9.17 0.0 7.8 Vet = 2.92 128.74 4.260 9.17 7. 9 7.9 A2 C=120 0.00 0.0 0.0 See PATH 5 AND 7 257.14 0.016 9.17 0.1 7. 9 Vel = 5.84 129.93 4 .260 9.19 8.0 8.0 A3 C=120 0.00 0.0 0.0 See PATH 8 AND 9 387 .07 0.034 9.19 0.3 8 .0 Vel = 8.80 132.45 4 .260 9.15 8.3 8.3 A4 C=120 0.00 0.0 0.0 See PATH 10 AND 11 519.53 0.059 9.15 0.5 8.3 Vel = 11.81 136.67 4.260 9.17 8 .9 8.9 A5 C=120 0.00 0 .0 0.0 See PATH 12 AND 13 656.19 0.090 9.17 0.8 8.9 Vel = 14.92 24.79 4.260 1E 7 .49 9.7 9.7 A6 C=120 13.17 0.0 0.0 See PATH 14 680 .98 0.097 20. 66 2.0 9.7 Vel = 15.48 6.357 lE 39.46 11.7 11.7 A7 C=120 1T 55.32 7.8 0.0 680. 98 0.014 94 .78 1.3 11.7 Vet = 6.95 A8 680. 98 20.8 K = 149.30 PATH 5 FROM HYDRAULIC REFERENCE 61 TO A2 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawlna Date:9-21-12 9123112 22:28 Tyco Fire Products Page 9 HYD. 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FITTING PIPE Pt Pt REF rrCrr TYPES FTNG"S Pe Pv ******* NOTES ******* L TOTAL Pf Pn PATH 5 FROM HYDRAULIC REFERENCE 61 TO A2 CONTINUED 21.31 2.157 9.25 7.1 7,1 K = 8.00 61 C=120 0.00 0.0 0.0 21.31 0.004 9.25 0.0 7 .1 Vel = 1.89 21.37 2.157 9.25 7.1 7�1 K = 8.00 62 C=120 0.00 0.0 0.0 42.. 67 0.016 9.25 0.1 7.1 Vel = 3.78 21.58 2.157 1T 5.45 7.3 7.3 K = 8.00 63 C=120 12.31 0.0 0.0 64 .25 0.034 17.75 0.6 7 .3 Vel = 5.70 A2 64.25 7.9 K = 22 .89 PATH 6 FROM HYDRAULIC REFERENCE 59 TO Al 21.33 2.157 9.25 7.1 7.1 K = 8 .00 59 C=120 0.00 0.0 0.0 21.33 0.004 9.25 0.0 7 .1 Vel = 1.89 21.39 2.157 9.25 7 .1 7.1 K = 8.00 58 C=120 0.00 0.0 0.0 42.71 0.016 9.25 0.1 7 .1 Vel = 3.79 21.60 2 .157 1T 3.80 7.3 7.3 K = 8 .00 57 C=120 12.31 0.0 0.0 64.32 0.034 16.11 0.5 7.3 Vel = 5.70 Al64.32 7.8 K = 22. 98 PATH 7 FROM HYDRAULIC REFERENCE 66 TO A2 21.38 2.157 9.25 7.1 7 .1 K = 8.00 66 C=120 0.00 0.0 0.0 21.38 0.004 9.25 0.0 7 .1 Vel = 1.90 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW ;GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 9123112 22:28 Tyco Fire Products Page 10 HYD. 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FITTING PIPE Pt Pt REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* Pn PATH 7 FROM HYDRRAULIC REFERENCE 66 TO A2 CONTINUED 21.44 2.157 9.25 7.2 7.2 K = 8.00 65 C=120 0.00 0.0 0.0 42.82 0.016 9.25 0.1 7.2 Vel = 3.80 21.66 2.157 1T 3.80 7.3 7.3 K = 8.00 64 C=120 12.31 0.0 0.0 64.48 0.034 16.11 0.5 7.3 Vel = 5.72 A2 64.48 7.9 K = 22. 98 PATH 8 FROM HYDRAULIC REFERENCE 67 TO A3 21.50 2.157 9.25 7.2 7.2 K = 8.00 67 C=120 0.00 0.0 0.0 21.50 0.004 9.25 0.0 7.2 Vel = 1. 91 21.56 2.157 9.25 7.3 7 .3 K = 8.00 68 C=120 0.00 0.0 0.0 43.07 0.016 9.25 0.1 7.3 Vel = 3.82 21 .78 2 .157 1T 5.45 7.4 7.4 K = 8.00 69 C=120 12 .31 0.0 0.0 64 .85 0.034 17.75 0.6 7.4 Vel = 5.75 A3 64 .85 8 .0 K = 22. 90 PATH 9 FROM HYDRAULIC REFERENCE 72 TO A3 21.58 2.157 9.25 7 .3 7 .3 K = 8.00 72 C=120 0.00 0.0 0.0 21.58 0.004 9.25 0.0 7.3 Vel = 1. 91 21.64 2.157 9.25 7 .3 7.3 K = 8. 00 71 C=120 0.00 0.0 0.0 43.22 0.016 9.25 0.1 7.3 Vel = 3.83 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CARLAS PASTA Drawing Date:9-21-12 9123112 22:28 Tyco Fire Products Page 11 HYD. 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FITTING PIPE Pt Pt REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* TOTAL Pf Pn PATH 9 FROM HYDRAULIC REFERENCE 72 TO A3 CONTINUED 21.86 2.157 1T 3.80 7.5 7.5 K = 8.00 70 C=120 12.31 0.0 0.0 65.08 0.034 16.11 0.6 7.5 Vel = 5.77 A3 65.08 8.0 K = 22. 98 PATH 10 FROM HYDRAULIC REFERENCE 74 TO A4 21 . 92 2.157 9.25 7.5 7.5 K = 8.00 74 C=120 0.00 0.0 0.0 21. 92 0.005 9.25 0.0 7.5 Vel = 1.94 21.98 2.157 9.25 7.6 7. 6 K = 8.00 75 C=120 0.00 0.0 0.0 43.90 0.017 9.25 0 .2 7.6 Vel = 3.89 22.21 2.157 1T 5.45 7.7 7.7 K = 8 .00 76 C=120 12.31 0.0 0.0 66.11 0.036 17 .75 0. 6 7.7 Vel = 5.86 A4 66.11 8.3 K = 22 .90 PATH 11 FROM HYDRAULIC REFERENCE 79 TO A4 22.00 2.157 9.25 7.6 7 .6 K = 8.00 79 C=120 0.00 0.0 0.0 22 .00 0.005 9.25 0.0 7.6 Vel = 1 .95 22 .06 2.157 9.25 7.6 7.6 K = 8.00 78 C=120 0.00 0.0 0.0 44 .06 0.017 9.25 0.2 7. 6 Vel = 3.91 22 .28 2.157 1T 3.80 7.8 7.8 K = 8.00 77 C=120 12.31 0.0 0.0 66.34 0.036 16.11 0.6 7.8 Vet = 5.88 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) 11 CARLAS PASTA Drawing Date:9-21-12 9123112 22:28 Tyco Fire Products Page 12 HYD. Qa DIA. FITTING PIPE Pt Pt REF "C" TYPES FTNG'S Pe Pv ******* NOTESPOINT Qt Pf/ft TOTAL ******* Pf Pn A4 66.34 8 .3 K = 22.98 PATH 12 FROM HYDRAULIC REFERENCE 80 TO A5 22 .62 2.157 9.25 8.0 8.0 K = 8.00 80 C=120 0.00 0.0 0.0 22. 62 0.005 9.25 0.0 8.0 Vel = 2 .01 22.68 2.157 9.25 8.0 8.0 K = 8.00 73 C,=120 0.00 0.0 0.0 45.30 0.018 9.25 0.2 8.0 Vet = 4 .02 22. 91 2 .157 1T 5.45 8.2 8.2 K = 8.00 60 C=120 12.31 0.0 0.0 68.21 0.038 17.75 0.7 8.2 Vel = 6.05 A5 68 .21 8. 9 K = 22.90 PATH 13 FROM HYDRAULIC REFERENCE 82 TO A5 22 .70 2.157 9.25 8.1 8.1 K = 8.00 82 C=120 0.00 0.0 0.0 22 .70 0.005 9.25 0.0 8.1 Vet = 2.01 22 .76 2.157 9.25 8.1 8.1 K = 8.00 81 C=120 0.00 0.0 0.0 45.46 0.018 9.25 0.2 8.1 Vet = 4.03 22 .99 2.157 1T 3.80 8.3 8.3 K = 8.00 53 C=120 12.31 0.0 0.0 68.45 0.038 16.11 0.6 8.3 Vel = 6.07 A5 68.45 8.9 K = 22.98 PATH 14 FROM HYDRAULIC REFERENCE 83 TO A6 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CAPLAS PASTA Drawing Date:9-21-12 9/23/12 22:28 Tyco Fire Products Page 13 HYD. Qa DIA. FITTING PIPE Pt Pt REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* POINTQt Pf ft TOTAL Pf Pn PATH 14 FROM HYDRAULIC REFERENCE 83 TO A6 CONTINUED 24.79 2 . 157 1T 3.80 9.6 9.6 K = 8.00 83 C=120 12.31 0.0 0.0 24.79 0.006 16.11 0.1 9. 6 Vel = 2.20 A6 24 .79 9.7 K = 7.96 PATH 15 FROM HYDRAULIC REFERENCE 84 TO B1 30.35 2 . 635 8.37 14.4 14.4 K = 8.00 84 C=120 0.00 0.0 0.0 30.35 0.003 8 .37 0.0 14.4 Vel = 1.80 30.38 2. 635 8.75 14.4 14 .4 K = 8.00 85 C=120 0.00 0.0 0.0 60.73 0.011 8 .75 0.1 14.4 Vel = 3.61 30.49 2. 635 8.75 14.5 14 .5 K = 8.00 86 C=120 0.00 0.0 0.0 91.22 0.024 8.75 0.2 14.5 Vel = 5.42 30.71 2. 635 8.75 14.7 14 .7 K = 8.00 87 C=120 0 .00 0.0 0.0 121.93 0.042 8 .75 0.4 14 .7 Vel = 7.24 31.09 2.635 lE 18.34 15.1 15.1 K = 8.00 88 C=120 8.24 0.0 0.0 153.02 0 .063 26.58 1.7 15.1 Vel = 9.09 4 .260 1T 7.00 16.8 16.8 103 C=120 26.33 3.0 0.0 153.02 0.006 33.33 0.2 16.8 Vel = 3.48 B1 153.02 20.0 K = 34 .20 PATH 16 FROM HYDRAULIC REFERENCE A9 TO A10 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) 11 C.ARLAS PASTA Drawing Date:9-21-12 9123112 22:28 Tyco Fire Products Page 14 HYD. Qa DIA. FITTING PIPE Pt Pt REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* TOTAL Pf Pn PATH 16 FR0M HYDRAULIC REFERENCE A9 TO A10 CONTINUED 201.39 6.357 2.71 19.5 19.5 A9 C=120 0 .00 0.0 0.0 See PATH 1 201.39 0.001 2.71 0.0 19.5 Vel = 2.06 -50.45 6.357 14 .00 19.5 19.5 C4 C=120 0.00 0.0 0.0 See PATH 17 150. 94 0.001 14 .00 0.0 19.5 Vel = 1.54 -50.35 6.357 14 .00 19.5 19.5 C3 C=120 0.00 0.0 0.0 See PATH 18 100.59 0.000 14 .00 0.0 19.5 Vel = 1.03 -50.29 2.157 1T 120.17 19.6 19. 6 C2 C=120 12.31 0.0 0.0 See PATH 19 50.30 0.021 132.48 2.8 19. 6 Vel = 4.46 2.157 14 .00 22 .4 22.4 22 C=120 0.00 0.0 0.0 50.30 0.021 14 .00 0.3 22.4 Vel = 4.46 2.157 13. 67 22 .7 22.7 23 C=120 0.00 0.0 0.0 50.30 0.021 13.67 0.3 22.7 Vel = 4 .46 2.157 14.00 23.0 23.0 1 C=120 0.00 0.0 0.0 50.30 0.021 14 .00 0.3 23.0 Vel = 4 .46 2 .157 13.00 23.3 23.3 21 C=120 0.00 0.0 0.0 50.30 0.021 13.00 0.3 23.3 Vel = 4.46 2.157 1T 101.89 23.6 23.6 4 C=120 12.31 0.0 0.0 50.30 0.021 114 .20 2.4 23. 6 Vel = 4 .46 50.29 6.357 1.37 26.0 26.0 E3 C=120 0 .00 0.0 0.0 See PATH 19 100.59 0.000 1.37 0.0 26. 0 Vel = 1.03 6.357 12.63 26.0 26.0 E4 C=120 0.00 0.0 0.0 100.59 0.000 12 . 63 0.0 26.0 Vel = 1.03 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE- (PSI)- - CARLAS PASTA Drawing Date:9-21-12 9123112 22:28 Tyco Fire Products Page 15 HYD. Qa DIA. FITTING PIPE Pt Pt REF licit TYPES FTNG'S Pe Pv ******* NOTES * ***** TOTAL Pf Pr_ PATE 16 FROM HYDRAULIC REFERENCE A9 TO A10 CONTINUED 50.35 6.357 14.00 26.0 26.0 E5 C=120 0.00 0.0 0.0 See PATH 18 150.94 0.001 - 14.00 0.0 26.0 Vel = 1.54 50.45 6.357 2.71 26.0 26.0 E6 C=120 0.00 0.0 0.0 See PATH 17 201.39 0.001 2.71 0.0 26.0 Vet = 2.06 A10 201.39 26.0 K = 39.47 PATH 17 FROM HYDRAULIC REFERENCE C4 TO E6 50.45 2.157 2T 276.73 19.5 19.5 C4 C=120 24 .61 0.0 0.0 See PATH 16 50.45 0.022 301.34 6.5 19.5 Vel = 4.47 E6 50.45 26.0 K = 9.89 PATH 18 FROM HYDRAULIC REFERENCE C3 TO E5 50.35 2 .157 1T 134.16 19.5 19.5 C3 C=120 12.31 0.0 0.0 See PATH 16 50.35 0.021 146.47 3.1 19.5 Vel = 4.46 2 .157 1T 142.56 22.7 22.7 3 C=120 12.31 0.0 0.0 50.35 0.021 154.87 3.3 22.7 Vel = 4.46 E5 50.35 26.0 K = 9.87 PATH 19 FROM HYDRAULIC REFERENCE C2 TO E3 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) CAPLAS F.ASTA Drawing Date:9-21-12 9123112 22:28 Tyco Fire Products Page 16 HYD. Qa DIA, FITTING PIPE Pt Pt REF "C" TYPES FTNG'S Pe Pv ******* NOTES ******* POINT Qt t TOTAL Pf Pn PATH 19 FROM HYDRAULIC REFERENCE C2 TO E3 CONTINUED 50.29 6.357 14.00 19.6 19.6 C2 C=120 0.00 0.0 0.0 See PATH 16 50 .29 0.000 14 .00 0.0 19.. 6 Vel = 0.51 2.157 1T 120.17 19.6 19. 6 Cl C=120 12.31 0.0 0.0 50.29 0.021 132.48 2.8 19. 6 Vel = 4.46 2.157 14 .00 22.4 22.4 18 C=120 0.00 0.0 0.0 50.29 0.021 14.00 0.3 22.4 Vel = 4.46 2.157 13. 67 22.7 22.7 19 C=120 0.00 0.0 0.0 50.29 0.021 13.67 0.3 22.7 Vel = 4.46 2.157 14 .00 23.0 23.0 2 C=120 0.00 0.0 0.0 50.29 0.021 14 .00 0.3 23.0 Vet = 4.46 2.157 13.00 23.3 23.3 17 C=120 0.00 0.0 0.0 50.29 0.021 13.00 0.3 23.3 Vet = 4.46 2.157 1T 101.89 23.6 23.6 104 C=120 12.31 0.0 0.0 50.29 0.021 114 .20 2.4 23. 6 Vel = 4.46 6.357 0.88 26.0 26.0 El C=120 0.00 0.0 0.0 50.29 0.000 0.88 0.0 26.0 Vel = 0.51 6.357 13 .12 26.0 26.0 E2 C=120 0.00 0.0 0.0 50.29 0.000 13.12 0.0 26.0 Vel = 0.51 E3 50.29 26.0 K = 9.86 UNITS - DIAMETER (INCH) LENGTH (FOOT) FLOW (GPM) PRESSURE (PSI) Job Waiter Required Hose Allowance CARLAS PASTA Static Pres: .34.0 psi Pressure: 52.4 psi In: 0 gpm 50 TALBOT LANE Resid. Pres: 68.0 psi Sys Flow: 1000 gpm Out 500 gpm ,r SOUTH WINDSOR, CT. 06074 Flow: 1280 gpm Sys+Hose: 1500 gpm Remote Area: 5 Date: 7-10-12 Safety Pres: 10.1 psi Loc: ON SITE Hd Eiv Pres: 14.7 psi 140 120 100 80 P Sup I S I 60 500 gpm hose 40 20 14.7 s' 300 450 600 750 900 1050 1200 1350 1500 Flog(anal)