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Home My WebLink About138 Commerce Way 21310 Plans Sprinklersaa r , ' r, ' BRAY aRf 1 N6Y COS FOR BUUW4 CONMUMON F • PWuiWG OESION ®Y COMPONENT P@p1 ORMANCE AP RO ACM aantartatsa ar raa oa nntaMr or aw+wrr wMr s AIR R E"IC& C1l- BEER - Q 1 a ICOP 1 Mwe" svmM TYPE - - TRIP Q MEAT KWA, OAS OIL Q SOLAR Q liE/ M10 EY EFFICIEN1C1l COP '(9 Gr Eppc&NCY o 8a.dY•wa) MOT V#M SYSTEM TYPE ELECTRIC p MEAT RECOVERY OAS OIL Q SOLAR k4 wall AMW I S ur Air — uo 101*00 Ir+p *Akw os z- 3 Z N. AMANA" Llo om Aow OTTIC. 4— OM vW AMW C" W asYm mil tq ANWAGM- _ OTTV rooNcailMq Actual DAM w M&007 F.L. 1 WOW am* taw go ptw aid POAM of ft arr and eva noia aoarrd tw urs croulntlon rid cau com- arowaon aw N aanprma wah MMf PoAOa irwBJ t %lo " FWM &WW co. "" oons mftn is comp V ttOftd. hWlm a via be WiwWdi to —in 'pp1 1— wo ssaAM F.S. i in -T -8fo GATE;--.-- CHECKEDby U11611blm 6 "WORKSHEET FOR ENERGY CALCULATIONS oU1LDIN i DE" Pr COMPONENT PERFORMANCE APPROACH Plali Wu ; IL1LL ° V - ,q C) M9 Lt T1 dE; _ eq.n TOTAL V,%SL AREA • i pq IL a .~010 w iin of rw doi omdoom, O000 oni 0 doasl ALAt. AI A BY 0AWffATM, 77. ar+aLr p _ CL 1111 TWT GNADM CLW TW SNAD ° co . I coamc wr y.. ... Mil _ TWAL n. TOTAL QLAU oLAM 000Ap omr ewe wONAW bm"m «r W o - • 2 sc n• y AC Wv mn 04 mow . ....................... r .......•.... a WT OIL WALL AM" MILL MML. QLAW MICA now~ mo opAom TlQIL) la4 IL) - (ia 11.) WALL AAEA 1o4 A) A.; .. ;.,;...:.. . L C. L Am FILM Ak F" kwidt Ak F" 1 ( p. i CRANED ',2Q0 3uf /yxz0 / 2 D ;ZVO (%dCT gip: CiE% 5Sve1 kT SERVING K. W. LOAD BREAKER WIRE CONDUIT DIS7 REMARKS. NO : A B C POLE TRIP NO. SIZE GYD. SIZI TYP AleI 5/ d ooylpe /6#TS 5 r ; SvlvX rov/r io 2 OF-C ,ri6Ts S' 42 1;7 A Z ALSp.9eE 747-AL t i t i I i I F. t i OFFICE AREA HYDRAULIC DESIGN INFORMATION SHEET NAME George Krieger DATE Dec 4 1986 LOCATION 138 Commerce Way Sanford Commerce Park BUILDING SYSTEM NO. CONTRACTOR Sun State Fire Sprinkler Co. CONTRACT NO. CALCULATED BY Sun State Fire Sprinkler Co DRAWING NO. o CONSTRUCTION: COMBUSTIBLE NON-COMBUSTIBLE CEILING HEIGHT FT. OCCUPANCY - Warehouse And Office NFPA 13: LT. HAZ. ORD. HAZ. GP. 1 2 3 EX. HAZ. NFPA 231 NFPA 231C: FIGURE CURVE Z OTHER (Specify) City Of Sanford SPECIFIC RULING MADE BY DATEw 0 w AREA OF SPRINKLER OPERATION Entire SYSTEM TYPE E- DENSITY • 10 WET DRY DELUGE PRE -ACTION AREA PER SPRINKLER 22 max SPRINKLER OR NOZZLE HOSE ALLOWANCE GPM: INSIDE 0 MAKE Central MODEL Pendent HOSE ALLOWANCE GPM: OUTSIDE 0 SIZE DT K-FACTOR 5-6 RACK SPRINKLER ALLOWANCE TEMPERATURE RATING 165 CALCULATION GPM REQUIRED 142.49 PSI REQUIRED 34.98 AT BASE OF RISER SUMMARY C" FACTOR USED: OVERHEAD_ 120 UNDERGROUND 150 y. WATER FLOW TEST DATES& TIME PUMP DATA RATED CAPACITY TANK OR RESERVOIR CAPACITY CL J STATIC PSI 2 AT PSI ELEVATION 0_ D RESIDUAL PSI 22 ELEVATION V) GPM FLOWING 1730 WELL w ELEVATION Same/site PROOF FLOW GPM H LOCATION Taken At Airport Blvd and commerce park area SOURCE OF INFORMATION City Of Sanford COMMODITY CLASS LOCATION w STORAGE HEIGHT AREA AISLE WIDTH O Q STORAGE METHOD: SOLID PILED % PALLETIZED % RACK % O SINGLE ROW CONVENTIONAL PALLET . AUTOMATIC STORAGE ENCAPSULATED y DOUBLE ROW SLAVE PALLET SOLID SHELVING NON- E MULTIPLE ROW OPEN ENCAPSULATED O Y O U ir FLUE SPACING IN INCHES CLEARANCE FROM TOP OF STORAGE TO CEILING FT. IN. O U LONGITUDINAL TRANSVERSE HORIZONTAL BARRIERS PROVIDED E45-1so u1 (10-76) HYDRAULIC CALCULATIONS Abbreviations C" Hazen & Williams Flow Value - - Line Calc" Branch Line Being Calculated Spkl." Number.of Sprinklers Being Calculated E.H.P." End Head Pressure Koo K Factor Q" Gallons Per Minute @ Specific Location Flow" Total Gallons Flowing Diam" Inside Diameter of Piping L/ft" Friction Loss Per Foot FF" Friction Loss Per Foot Lgth" Length of Piping Plus Fitting Loss Len" Length of Piping Plus Fitting Loss Loss" Friction Loss for Total Length PT" Pressure Total End P" Starting Pressure for Main Calculations P E" Pipe Elevation Loss Stat" Static Pressure Read" Residual Pressure Avail" Pressure Available @ System Demand Hydrant Outlet I.D. Pitot Press. Flow Residual Dater Time: Cont. No. No. Inches psi gpm psi 1 Cont. Name: Gecr e Krieger 2 Address: Sanford Commerce Park 3 Total Flow Static Press: psi Flow C- 20 psi9pm 120 115 110 9105 100 95 90 85 80 N 75 a 70 pv 65 S a 1 C P. 1. CL 60 55 50 45 c 40 35 sE 30 25 20 FFI E EM AD- 35.0 I P.S. I Res n1130 uLE 15 10 5 0 Scale. E ev rto Loss- 39R.S.I. Scale A 100 200 300 400 500 600 700 800 900 1000 Scale 8 200 400 600 800 1000 1200 1400 1600 1800 2000 Scale C 400 800 1200 1600 2000 2400 2800 3200 3600 The v;k;, g Cwpo jt;o 4000 Nntimgs, Mich;`an Water Flow gPm Utho 1 U.S.A. Fo,m No 3016 — HYDRAULIC CALCULATIONS SHHcir 01 . George Krieger Q Y Von OAS Office Area Line Cale Line Cale Line Cale Typical Drop for 1 Spkl Pts 6&8 1 Spkl 1 Sprk 7.42 Ehp 8.433 Ehp 7 Ehp 5.439 K 5.44 O K 14.81566029 Q+ 15.79755768 Q+ 5.6 K 14.81566029 Flow 15.79755768 Flow 14.81620734 Q+ 1.049 Diam L/ft 1.049 Diam 14.81620734 Flow 0494341248 14.17 Lgth 0556652784 L/ft 1.049 Diam Loss 9 Lgth 0494375016 L/ft 7004815478 8.120481548 Pt 5009875054 Loss 8.5 Lgth 8.933987505 Pt 420218737 Loss 14.81566029 Flow 7.420218764 Pt 8.120481548 Pt 15.79755768 Flow 8.933987505 Pt 14.81620734 Flow 5 199123329 K 5.285271231 K 7.420218764 Pt 5.439120649 K Line Cale Line Cale 1 Spkl 1 P Spkl Line Cale - DRo P 8.433 Ehp 8.5 s Ehp 9 ForQ PTS 1-9 1 Spkl 5.44 0 K 15.79755768 Q+ 16-32666531 Q+ ° 7.96 Ehp 15.79755768 Flow 16.32666531 Flow 1.049 Diam 1.049 Diam 5.6 K 0556652784 L/ft 0591634286 L/ft 15.7995443 Q+ 9 Lgth 17.375 Lgth 15.7995443 Flow 5009875054 Loss 1.027964573 Loss 1.049 Diam 8.933987505 Pt 9.527964573 Pt 0556782294 L/ft 8.5 lgth 15.79755768 Flow 16.32666531 Flow I 4732649495 Loss 8.933987505 Pt 9.527964573 Pt j 8.43326495 Pt 5.285271231 K 5.289290535 K 15.7995443 Flow 8.43326495 Pt Line Cale Riser Nipples s 5.440598638 K 1 Spkl For Pts 10& 11 7.42 Ehp 10.64 K 5.439 8 K 9.527 Pt 14.81566029 Q+ 32.8412524 Flow 14.81566029 Flow 1.38 0566937154 Diam L/ft 1.049 Diam L/ft 6.5 Lgth0494341248 11.25 Lgth 368091502 Loss 5561339035 Loss 9.89550915 Pt 7.976133903 Pt. 32.8412524 Flow 14.81566029 Flow - 9.89550915 Pt 7.976133903 Pt 10.44000335 K 5.245957807 K HYDRAULIC CALCULATIONS SHQ[T rom George Krieger BY - DATE Offi ee ArPa JOB NO - Riser Nipples Crossmain RISER Pts 6 & 7 End Pt 10.484 K 8.933 Pt 31-33470997 Flow 1.38 Diam 0519763719 L/ft 6.5 Lgth 3378464175 Loss 9.270846418 Pt 31.33470997 Flow 9.270846418 Pt 10.29119923 K Riser Nipples Pts 8 & 9 10.53 8.933 31.47219534 1.38 0523990575 6.5 3405938738 9.273593874 31.47219534 9.273593874 10.33482202 Line Calc 1 8.5 5.6 16-3266581 16-3266581 1.049 0591634286 13.625 8061017152 9.306101715 16-32666531 9.306101715 5.351969038 K Pt Flow Diam L/ft Lgth Loss Pt Flow Pt K Spkl Ehp It K Q+ Flow Diam L/ft Lgth Loss Pt Flow Pt K 10.291 31- 332672:93 31-33267293 1.38 0519701211 12 6236414528 9.893641453 10.334 32.50472835 63.83740128 1.38 19388650 11.67 2.262655468 12.15629692 10.334 36-03040193 99.86780321 1.38 4437063294 10.17 4.51249337 16.66879029 10.44 42.62383678 142.49164 1.61 4042387585 36.687 14.83030733 31.49909762 0 0 142.49164 4.26 0035371642 2.58 0091258836 31.50822351 9.27 OKQ+ Flow Diam L/ft Lgth Loss Pt OKQ+ Flow Diam L/ft Lgth Loss Pt OK Q+ Flcw Diam L/ft Lgth Loss Pt. OKQ+ Flow Diam L/ft Lgth Loss Pt K Q+ Flow Diam L/ft Lgth Loss Pt 142.49164 Flow 4.26 Diam 0035371642 L/ft 24 Lgth 0848919407 Loss 31-59311545 Pt 7.83 Elev 3.39039 Pe 34.98350545 Pt HOSE o RACK SPKL 0 BASE OF RISER 142.49164 Flow 34.98350545 Pt Undg Main C FACTOR 150 142.49164 Flow 6.09 Diam 0006205743 L/ft 184.08 Lgth 1142353C83 Loss 35-09774076 Pt Flow Test STAT 62 RESD 22 Flow 1730 142.491 Flowing 61.60537785 AVAIL 242.491 Flowing 60.94473483 AVAIL Warehouse Area HYDRAULIC DESIGN INFORMATION SHEET NAME _ George Kr LOCATION 13b Commerce Way Sanford Commerce Park BUILDING StCONTRACTORun ate Eire Sprinkler Co CALCULATED BY Sun State Fire Sprinkler Co. CONSTRUCTION: COMBUSTIBLE up NON-COMBUSTIBLE OCCUPANCY Warehouse and Office SYSTEM NO. CONTRACT NO. DRAWING NO. 1 Of 1 CEILING HEIGHT FT. NFPA 13: LT. HAZ. ORD. HAZ. GP. 1 2 Mg 3 EX. HAZ. NFPA 231 NFPA 231C: FIGURE CURVE C9 OTHER (Specify)_. C7 tv OP SPECIFIC RULING MADE BY DATEW 0 W AREA OF SPRINKLER OPERATION 1500 SYSTEM TYPE N DENSITY 21 IM WET DRY DELUGE 0 PRE -ACTION AREA PER SPRINKLER 130 Max SPRINKLER OR NO_ ZZLE. HOSE ALLOWANCE GPM: INSIDE 0 MAKE Central MODEL Upright HOSE ALLOWANCE GPM: OUTSIDE 500 SIZE 2 K-FACTOR 5.6 RACK SPRINKLER ALLOWANCE 0 TEMPERATURE RATING 165 ALCULATION GPM REQUIRED 351 259 PSI REQUIRED 38.88 AT BASE OF RISER. UMMARY C" FACTOR USED: OVERHEAD_ 120 UNDERGROUND 150 J WATER FLOW TEST DATE& TIME PUMP DATA RATED CAPACITY TANK OR RESERVOIR CAPACITY - STATIC PSI AT PSI ELEVATION RESIDUAL PSI 22 ELEVATION v' GPM FLOWING 1730 WELL LU ELEVATION Same/site PROOF FLOW GPM I- Q LOCATION Taken at Airport Blvd and commerce park SOURCE OF INFORMATION_ City Of Sanford COMMODITY CLASS LOCATION W STORAGE HEIGHT AREA AISLE WIDTH cc STORAGE METHOD: SOLID PILED % PALLETIZED 9'o RACK % O SINGLE ROW E] CONVENTIONAL PALLET AUTOMATIC STORAGE ENCAPSULATED DOUBLE ROW SLAVE PALLET SOLID SHELVING NON- MULTIPLE ROW OPEN ENCAPSULATED O Y O U Q FLUE SPACING IN INCHES CLEARANCE FROM TOP OF STORAGE TO CEILING O LONGITUDINAL TRANSVERSE FT. IN. U HORIZONTAL BARRIERS PROVIDED E45-ISO VI (lo-76) HYDRAULIC CALCULATIONS Abbreviations C" Hazen & Williams Flow Value Line Calc" Branch Line Being Calculated Spkl." Number of Sprinklers Being Calculated E.H.P." End Head Pressure K" K Factor Gallons Per Minute @ Specific Location Flow" Total Gallons Flowing Diam" Inside Diameter of Piping L/ft" Friction Loss Per Foot FF" Friction Loss Per Foot Lgth" Length of Piping Plus.Fitting Loss Len" Length of Piping Plus Fitting Loss Loss" Friction Loss for Total Length PT" Pressure Total End P" Starting Pressure for Main Calculations P E" Pipe Elevation Loss Stat" Static Pressure Resd" Residual Pressure Avail" Pressure Available @ System Demand WATER FLOW TEST SUMMARY SHEET Hydrant NO Pitot Press., Restdual 1, Date: Time: Cont. No. Cont. Name: Gecrae--Krieaer Address: P,2ry Total Flow•Flow 5) 20 • • 120 IIYYWYWYYWYWYWiYYYW111Y111Y11111WYWYYWYWWYWYYWWYYYWW 115 110 05 100 11 1 75 1 i la 55 20 15 ICY• 50 r®®is e®a eP- Al1 l I AAIAAA!!!!l1 111111111!l1111111111IAlAAIII R!A!!l11 1 Scale A 100 200 300 400 500 600 700 800 0- Scale B 200 400 600 800 1000 1200 1400 1600 S',t. (7 4nn Rnn 12nn 16nn 2nn0 2400 )Ann ??no 900 000 1800 2000 i Fnn _. .... . _ Anon CONTRACT NO. SFIEET NO 1 OF NAME; G oR K DATE Dtc. S. IqB LOCATION w,aQIE us _ L wIE , ! NOZZLE TYPE & LOCATION FLOW IN G.P.M. PIPE SIZE FITTING SI DEVICES PIPE EQUIV. LENGTH FRICTION LOSS PS -I -/FT REQUIRED P.S.I. HYD• REFPT 0 ELEV. NOTES g Ii1 H.9 I,o PT 1 olo1 I VC S•G® c=12oQ23•a9 FTG. I • s 5 TOT 9 2' 332LPE g 23.9z 1,4 LGTH. 9 Z' I 8 1 l `1 PT 18.243 2 Q'7•dl FTG- ._-. PF 1.5141 TOT. 9 2'2 PF -.332- P T 1 9. 5- 32`• l 1 2 LGTH. Q 1 1. "1 1 FT_G. — PF 1.6U T. q z' z PE3 3 2 Q 25.49 12 LGTH. 5_2i PT 2U•124, Lf Q,97. 2 FTG • r-Va-o PF T. 21•'2I PE Q LGTH. PT 21.o3 14: 18.495 Q `l l• Z TG• PF TOT. PE- 0 L H. PT 0 FTG . PF TOT PE 2 b Z IQ23.U9 FTG, r` PF TOT. z-v'z PE g LGTH • PT 5.52, T'of, of R.NQ23.09 FTG- PF TOT. PE g LGTH. PT Q FTG• PF TOT. PE g LGTH. PT Q FTG- PF TOT PE g LGTH- PT — Q FTG- PF TOT. PE g L UTH. PT Q FTG- PF TOT. PE g LGTH. PT Q FTG- PF TOT. PE Q LGTH _ PT Q FT . PF TOT. PE Q LGTH. PT Q FTG- PF TOT. PE oLGTH- PT Q FTG- PF TOT. PE o LGTH. PT Q FTG- _------ TOT. PF PE' o LGTH. _ pT Q FTGm PF TOT P PT r--,t .)ci rr<nvi HYDRAULIC CALCULATIONS 3HIff LCW 2 FOR George Krieger By Warehouse Area CAS JOB NO Crossmain Riser Nipples End Pt 28.764 Undg. Main C Factor 150 PtsA& B 23. 531 O K 351.2593616 Flow 24. 275 K 126.2016473 Q+ 6.09 Diam 27. 03 Pt 126.2016473 Flow 0032937833 L/ft 126. 2066565 Flow 4.26 Diam 184.08 Lgth 2. 067 Diam 0042697129 L/ft 9 7}15 1445264024L/ft 12 Lgth 39- Pt 12 Lgth 0512365551 Loss 1. 734316828 LOSS 28.81523656 PT Flow Test 28. 76 31683 Pt. 23. 531 O jK Stat 62 126. 2066565 Flow 126-3139972 Q+ Resd 22 28- 76431683 Pt 252-5156445 Flow Flow 1730 23- 53180439 K 4.26 Diam 0154050005 L/ft Lgth 351.259 Flowing 12. 25 1887112567 Loss 59-905 PT. Avail 29- 00394781 Pt 851. 259 Flowing Riser Nipples 51.22818524 Avail Pt C 18. 335 c K 18. 695 K 98-74371711 Q+ 27. 03 Pt 351.2593616 Flow 97. 19602238 Flow 4.26 Diam 2. 067 Diam 0283687377 L/ft L/ ft 86.04 Lgth 08914453412 Lgth 2.440846189 Loss 1. 069734409 Loss 31.444794 Pt 28. 09973441 Pt Riser O j 97-19602238 Flow 351.2593616 Flow 28- 09973441 Pt 4.26 Diam 18. 33569536 K 0283687377 L/ft 33. 25 Lgth 9432605273 Loss 32. 38805453 Pt 15 Elev 6. 495 Pe 38. 88305453 Pt Hose 0 Rack Spkl 0 BASE OF RISER 351. 2593616 Flow 38. 88305453 Pt pr>o va.-ho ,s -ror 67,eo9 e- )<rl2Jc e--r 138 (',pmmP.ce.Vj 61-Y 70d /,3/ 0