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312 W 1 St - NO PERMIT # (FIRST FEDERAL OF SEMINOLE) (FIRE) DOCUMENTSNTON FIRE SPRINKLERS P. 0. Box D LONGWOOD, FLORIDA 32750 Phone A/C (305) 831-3414 TO City of Sanford FjrP Department 14th. Greet &-Fresh Sanford, Florida —3 27 DATE JOB NO.. A ATTENTION RE: First Federal nf qemjnnli 312 West First Street Sanford GENTLEMEN: WE ARE SENDING .YOU .. EX Attached Under separate cover via the following items: Shop drawings Prints Plans Samples Specifications Copy of letter Change order COPIES DATE NO. DESCRIPTION 4-2-81 1 DrawinclsShop THESE ARE TRANSMITTED as checked below: X 1. REMARKS For approval For your use As requested For review and comment FOR BIDS DUE After your review, Approved as submitted Approved as noted. Returned for corrections. 19 please place your stamp Resubmit copies for approval Submit copies for distribution Return corrected prints PRINTS RETURNED AFTER LOAN TO US of approval and/or comments on two (2) sets, so that we may' have one (1a for the hi,; l d; ng department for a 3—r permit applicatio i to call our office.. COPY TO SIGNED: FORM 2403 Avfllle6le from Groton, Mass. a1450 - r If enclosures are not noted, kindly. notify us at once. Diane WIGINTON FIRE SPRINKLERS P. 0. Box D LONGWOOD, FLORIDA 32750 Phone A/C (305) 831-3414 TO Ci tv n ford Btiu 1-ding Deparbm6nt CityHall -I P0. Box 1778 N. Sanford, F1 32771 GENTLEMEN: WE ARE SENDING YOU [X Attached Under separate cover via the following items: Shop drawings Prints Plans Samples Specifications Copy of letter 0-Change order . N Necessary' information for __rmit app!irati= DATE JOB NO. - 81039 ATTENTIO RE: First Federal of Seminole 312 West First Street Sanford, FL , 32771 COPIES. DATE NO. DESCRIPTION 2 4- 2-8 1 Co ' 1 Our cost of this project is $11,900.00), THESE ARE TRANSMITTED as checked below: For approval Approved as submitted Resubmit copies for approval f For your use Approved as noted Submit copies for distribution As requested Returned for corrections Return corrected prints El For review and comment FOR BIDS DUE 19 PRINTS RETURNED AFTER LOAN TO US REMARKS Plp_ a-au- be advised that thiiz_ General CGntx-acterls permit en tahas project is 1#14641_ Williams Develo tir the above referenced pmjet, and Liar, for Game If gym„ ahni,ld have any questions, pleasP- do not hesitate to call our office COPY FORM 240- 3 Available from A a Groton, Mass.01450' SIGNED: If enclosures are not as noted, kindly notify us at once:, Diane Lewis STATE OF FLORIDA- DEPARTMENT OF INSURANCE AND TREASURER TALLAHASSEE, FLORIDA SINES a F y 4 4 STATE FIRE MARSHAL $ u - CERTIFICATE OF CMMPITENCY THIS CERTIFIES THATI J0F5 E WIGINTON LU;vGWSOgDELORInA 32750 QUALIFIV TO ENGAGEHIN THE BU INEgS 0 CM TRAUTfNGI pR FIREAPROTE T 0 1 SYSTEMS 0 WIGINTON FIRE SPRINKLERS INC INSURA E COMMISSIONER071011800711010010897350278-00 0087106 07500 06 30 81 TREASURER AND STATE ISSUE DATE TYPE CLASS OU.T LICENSE OR PERMIT NUMBER APPLICATION TAXES 6 FEES COMPANYT EXPIRATION FIRE MARSHAL CODE DATE CITY OF SANFORD. FLORIDA CHECK Q[ M. 0- 0 CASH 13 SUBJECT TO SUSPENSION OR MUST BE POSTED 0 REVOCATION IN ACCORDANCE IN A CONSPICLX%JS PLACE 0 1 10 0W, I TH ORDINANCES OF SAID CITY CITY REGISTRATION N THE PLACE OF BUSINESSN- CF-RTIFICATF- EXPIRES91-30-19 25% PENALTY IF NOT RENEWED BY NOV. 1 $10.10 WIGINTON FIRE, SPRIIMERS, INC P.O. BOX D LONGWOOD, FLA. 32750 This form becomes a RECEIPT ONLY when validated by recelPtin-9 ftmachineshowingDATEANDANOUNTPAID. JOE W. WIGINTON j- FIRE PROTECTION SYSTEMS% Specialty) G'Ofiti 2 6 PLEASE MAKE REMITTANCE TO: H. N. TAMM JR., City Tax Collector CITY OF SANFORD, FLORIDA 32771 00:: ..04)))) ((((Oo.. .:00.. 0: .:0: :O:)))))V(((((:O: :0:. :0:. 0: .:0: :0:. :0:. 00) (00) (00) wwwwwww (Cl 0) (00) (00) DOO) (000) (000) wwwwwww (000) (000) (000) wwwwwww WWWWWWw wwwwwww wwwwwww WWWWWWw T WWUIWWWw T Wwviwwww wwwwwww TT wwwwwww TT wwwwwww wwwwwww ttt wwwwwww ttt wwwwwww wwwwwww T ttttt wwwwwww ttttt T wwwwwww wwwwwww TT TTTT) (T) wwwwwww (T) (TTTT ft wwwwwww wwwwwww ( t t t •t T T? T S t T) wwwwwww ( T T t T t T t t T T T) wwwwwww wwwwwww (ttttttttt) wwwwwwwww (TTTTTTttt) wwwwwww wwwwwww (ttttttT) wwwww wwwww (ttttttT) WWWWWWW WWWWWWWWWWwWWWWWWWWWWw wWWWWWWWWWWwWWWWWWWWWW WWWWWWWWWWWWWWWWWWW wwwwwwwwwwwwwwwwwww wWwwwwwwwwwww WWWWWWWWWWWWvi F= i F- o- -IF u r--1-v s U s. O T-s mo t -:W --";u -* -3"U -* -3-U -t- tea- -* -* -31* - -* --i -:-L- -3* -* -* tea- -s- -* -3*- -3* -:W -3*- 3 W I C,- I "i C3 9"tit F= I FREE !:-:; P FR I "K i_ E F;Z !EB - LC "c,- WC3OiD F= LLB, - _7=3Z-7 5 D 3<D5—:E3 :31-41rt x--- CONTRACTOR WIGINTON FIRE SPRINKLERS , INC. # NAME FIRST FEDERAL OF SEMINOLE # LOCATION SANFORD FLORIDA # SYSTEM NO. 1 # CONTRACT NO. 81039 # W I C3 I P%1T(3rd F= I RE !E3P FZ I r%JKLERS ,'YI HYDRAULSC DESIGN INFORMATION SHEET=====__________________ NAME FIRST FEDERAL OF SEMINOLE DATE 4/6/81 LOCATION SANFORD , FLORIDA BUILDING OFFICE BLDG. SYSTEM NO. 1 i CONTRACTOR WIGINTON FIRE SPRINKLERS , INC. CONTRACT NO. 81039 CALCULATED BY G.W.S. DRAWING NO. 1 OF 1 CONSTRUCTION:( )COMBUSTIBLE (X)NON-COMBUSTIBLE CEILING HEIGHT 9-0 OCCUPANCY OFFICE BLDG. i S !(X)NFPA13 (X)LT.HAZ. ORD. HAZ.GP.( )1( )2( )3( )EX.HAZ. Y !t )NFPA 231 ( )NFPA 2_31C FIGURE CURVE ` S !( )OTHER T !( )SPECIFIC RULING MADE BY DATE E M !AREA OF SPRINKLER OPERATION 1S00 SYSTEM TYPE DENSITY=GAL/MIN/SG.FT .1 (X)WET( )DRY( )DELUGE( )PREACTION D !AREA PER SPRINKLER 214 SPRINKLER OR NOZZLE r E 'HOSE ALLOWANCE GPM -INSIDE 750 MAKE RELIABLE MODEL G S !HOSE ALLOWANCE GPM -OUTSIDE 0 SIZE 112 K-FACTOR S.62' I !RACK SPRINKLER ALLOWANCE 0 TEMPERATURE RATING 16S G '. N ! CALCULATION ! GPM REQUIRED 979 PSI REQUIRED 101.S3 AT BASE OF RISER -E SUMMARY ! C FACTOR USED: OVERHEAD 120 UNDERGROUND 140 W_!WATER ^FLOW TEST PUMP DATA '====TANK OR RESERVOSR A !DATE & TIME ! RATED CAP 7S0 ! CAP. 0 T !STATIC PSI 60 ! AT PSI 7S ! ELEV. 0 E !RESIDUAL PSI 40 ! ELEV 2.S ! R !GPM FLOWING 1060 ! ! WELL ELEVATION 2.S ! ! PROOF FLOW GPM 0 IS U!_________________________________________________________________________ P ! P !LOCATION :SEE PLANS L !SOURCE OF INFORMATION :SEE PLANS ' Y ! COMMODITY CLASS LOCATION j C !STORAGE HT. AREA AISLE WIDTH 0 !STORAGE METHOD:SOLID PILED % PALLETIZED % RACK % M M ! ! ( )SINGLE ROW( )CONVENTIONAL PALLET( )AUTOMATIC STORAGE( )ENCAPSULATED R ! ( )DOUBLE ROW( )SLAVE PALLET( )SOLID SHELVING( )NON -ENCAPSULATED S ! A ! ( )MULTIPLE ROW ( )OPEN T ! G 0 ! K ! FLUE SPACING IN INCHES: CLEARANCE:STORAGE TO CEILING R ! ! LONGITUDINAL TRANSVERSE FT. A G ! ! HORIZONTAL BARRIERS PROVIDED: E F= 11 RE F='FZOTFEE C--T I C3 - -E3`e ir- C3 M F:l UTER CDE!E; I C;;N VJ = CA a rv-ror4 F = FTEO E3FAFR z PaKL-E=FZA3 , = PQCD JOB- FIRST FEDERAL OF SEMINOLE JOB NO 81039 DATE 4/E 81 PAGE 1 SPRKLR. GA C" EGUIV. PIPE PT PT IDENT. FLOW DIA. FITTING FTGS. PE PV#### NOTES ##### GT LOSS/FT LENGTHS TOT. PF PN 14.9 1.049 pE 2.0 3.00 7.00 G=K*SGR(P):P= 7 1 1 C=120 IT 5.0 5.00 0.00 K= 5.620 14.9 0.0754 8.00 0.60 14.9 7.60 K 10= 5.40 1 -T 14. 9 1.049 6.00 7.00 G=K*SGR (P) : P= 7 2 1 C=120 0.00 0.00 K= 5.620 14.9 0.0754 8.00 0.60 15.2 1.380 OE 3.0 9.50 7.60 7.60 K= S.620 P= 7. 32 2 2 C=120 1T 6.0 6.00 0.00 0.28 G= 30.1 IN 1.380"1 30.1 0.0729 15.50 1.13 7.32 30.1 8.73 K 11= 10.19 2 T r 14.9 1.049 IE 2.0 11.00 7.00 G=K*SGR(P):P= 7 3 1 C=120 2.00 0.00 K= 5.620 14.9 0.0754 13.00 0.98 10----------------------------- 15.0 1.380 1 E 3.0 13. 50 7.98 7.98 K= 5.400 P= 7.70 3 2 C=120 3.00 0.00 0.28 G= 29.9 IN 1.320' 29.9 0.0720 16.50 1.19 7.70 16.7 1.610 7.00 9.17 9.17 K= 5.620 P= 8.81 3 3 C=120 0.00 0.00 0.36 G= 46.6 IN 1.610'' 46.6 0.0772 7.00 0.54 8.81 31..1 2.068 5.00 9.71 3.71 K= 10.190 P= 9. 34 3 4 C=120 0.00 0.00 0.37 G= 77.7 IN 2.OE8"I 77.7 0.0587 5.00 0.29 9.34 j 17.3 2.068 1 E 5.0 11. 50 10.00 10.00 K= 5.620 P= 9.44 3 5 C=120 5.00 0.00 0. 56 G= 95.0 IN 2.068" 95.0 0.0852 16.50 1.41 9.44 I 18.3 2.068 12.00 11.41 11.41 K= 5.620 P= 10.626 3 E, C=120 0.00 0.00 0.79 G= 113.3 IN 2.068"; 113.3 0.1180 12.00 1.42 10.62 19.3 2.068 OE 5.0 13.00 12.83 12.23 K= S.620 P= 11.75i 3 7 C=120 1T10.0 10.00 0.00 1.08 G= 132.6 IN 2.066' 132.6 0.1579 23.00 3.63 11.75 132.6 7----------------------------------- 16.46 K 12= 32.68 t3T 3s# WI<,Ir-,J `1 FIFE S IRI"KLEFZ I1 C JOB- FIRST FEDERAL OF SEMINOLE JOB NO 81039 DATE 4/6/81 PAGE 2-i DESIGN AREA 1#### HYDRLC. GA DIA. EQUIV. PIPE PT PT REF. FLOW C" FITTING FTGS. PE PV NOTES I POINT QT LOSS/FT LENGTHS TOT. PF PN I 21.4 1.049 .14.29 14.55 Q=K*SQR(P):P= 14.55 4 1 C=120 0.00 0.00 K= 5.620 21.4 0.1474 14.29 2.11 21. 7 1.049 3.17 1 E.. 66 1 E.. 6E. K = 5.620 P= 14.93 4 2 C=120 0.00 0.00 1.73 Q= 43.1 IN 1.049" 43.1 0. 5385 3.17 1.71 14.93 132.E 2.068 11.13 18.37 18.37 K= 32.680 P= 16.47 4 3 C=120 0.00 0.00 1.90 Q= 175.7 IN 2.068" ' 175.7 0.2653 11.13 2. 96 16.47 24.4 2.OEZ OE S.0 4.13 21.33 21.33 K= 5.620 P= 18.8E 4 4 C=120 IT10.0 10.00 0.00 2.47 Q= 200.1 IN 2.068" 200.1 0.3392 14.13 4.78 IS. BE, 200.1 26.11 K 13= 39.16 4 -T 0.0 1.049 14.29 14.98 QA= 0.0 PT= 14.98 5 1 C=120 0.00 0.00 0.0 0.0000 14.29 0.00 0.0 1.04.3 14.29 14.98 GA= 0.0 PT= 14.93 5 2 C=120 0.00 0.00 Q= 0.0 IN 1.049" 0.0 0.0000 14.29 0.00 21. 6 1.380 OE 3.0 4.13 14.98 14.98 K= 5. 620 P= 14.83 S 3 C=120 IT 6.0 6.00 0.00 0.15 Q= 21.6 IN 1.380" 21. E, 0.0394 10.13 0.40 14.83 21.6 15. 38 K 14= 5. S1 5 T 200.1 2.157 15.00 26.11 GA= 200.1 PT= 26.11 CM C=120 0.00 0.00 200.1 0.2754 IS.00 4.13 28."3 2.157 42.58 30.24 30.24 K= 5.510 P= 27.51 CM C=120 31.00 0.00 2.73 Q= 229.0 IN 2.157" 229.0 0.3535 31.00FT 73.58 26.02 27.51 229. 0 56. 2E K 1 S= 30.53 CM 229.0 4.02E, 0.00 56.26 QA= 229.0 PT= 56.26 STOP C=120 0.00 0.00 ' 229.0 0.0169 0.00 0.00 3t--3* -3* W I C- I NT C3 F= I FR E SF=> FZ I L__EFZ S v I NC _ -3*-3* -3* -3* JOB- FIRST FEDERAL OF SEMINOLE JOB NO 81039 DATE 4/6/81 PAGE 3 tt#it#######DESIGN AREA #1#;tttit#tt#tt, HYDRLC. GA DIA. EQUIV. PIPE PT PT REF. FLOW C" FITTING FTGS. PE PV NOTES ### POINT QT LOSS/FT LENGTHS TOT. PF PN SOO.0 4.026 72.00 SS.2E, GA= SOO.0 PT= S6.26 STDP C=120 0.00 32.30 Q= 729.0 IN 4.026" 729.0 0.1441 72.00 10.38 PE=.4331X 74.57' 98.94 K 16= 73.29 STDP 729.0 8.071 0.00 98.94 GA= 729.0 PT= 99.94' UDG C=120 0.00 0.00 729.0 0.0048 0.00 0.00 2SO.0 8.071 42.00 98.94 GA= 2SO.0 PT= 98.941 UDG C=120 100.00 0.00 Q= 979.0 IN 8.071" 979.0 0.0084 100.00FT 142.00 1.19 979.0 100.13 K 17= 97.84 UDG e---------------------------------------------- I DENSITY X AREA 0.100 X 1500.0 = 150.00 OVERAGE = 49.20 GPM = 49.20 RACKS = 0.00 INSIDE HOSES = 7SO.00 OUTSIDE HOSES = 0.00 FLOW REG'0 FOR SYSTEM = 199.20 FLOW AT BASE OF RISER = 949.20 MIN FLOW AT BASE OF RISER = 949.20 TOTAL FLOW = 949.20 STATIC PRESSURE = 60.00 RESIDUAL PRESSURE = 41.11 RESIDUAL FLOW = FLOW FROM CITY SUPPLY AT 20PSI = 1424 GPM PUMP RATING 75.00 PSI AT 7SO.00 GPM PRESSURE FROM CURVE @ TOTAL FLOW = ELEVATION = 2.S2 FT = NO. DIA "C" LENGTH FACTOR ADDITIONAL VALVE LOSS, ETC. SAFETY MARGIN (IN PSI) PRESSURE AVAILABLE FOR SYSTEM k VA, l C___ 949.20 103.72 1.09 FLOW PF 0.00 0.00 104.81 FLOW DENSITY X AREA 0.100 X 1500.0 = 150.00 OVERAGE = 49.20 GPM = 49.20 RACKS = 0.00 INSIDE HOSES = 750.00 OUTSIDE HOSES = 0.00 FLOW REG'D FOR SYSTEM = 199.20 FLOW AT LASE OF RISER = 949.20 MIN FLOW AT SASE OF RISER = 949.20 TOTAL FLOW = 949.20 STATIC PRESSURE = 60.00 RESIDUAL PRESSURE = 40.00 RESIDUAL FLOW = 1060.00 FLOW FROM CITY SUPPLY AT 20PSI = 1542 GPM PRESSURE FROM CURVE @ TOTAL FLOW 43.69 ELEVATION = 0.00 FT 0.00 NO. DIA "C" LENGTH FACTOR FLOW PF FLOW 1 7.980 140 408.00 G IH 0.0 2.56 949.20 ADDITIONAL VALVE LOSS, ETC. 0.00 SAFETY MARGIN (IN PSi) 0.00 PRESSURE AVAILABLE FOR SYSTEM 41.11 --.qt 3* # -3* tr l I C3 I "-IF C3" F- I FREE EF' FR I Ni-C L EFL S . I "C _ - - JOB- JOB NO DATE PAGE 1 DESIGN AREA 2### SPRKLR. GA licit EQUIV. - PIPE PT PT IDENT. FLOW DIA. FITTING FTGS. PE PV NOTES #### QT LOSS/FT LENGTHS TOT. PF PN 21.4 1.049 14.29 14.55 Q=K*SQR(P):P= 14.55 1 1 C=120 0.00 0.00 K= 5.620 21.4 0.1474 14.29 2.11 21.7 1.049 14.29 1 E.. 66 16.66 K= S. E,20 P = 14.93 1 2 C=120 0.00 0.00 1.73 Q= 43.1 IN 1.049" 43.1 0.5325 14.29 7.70 14.93 26.9 1.380 14.29 24. 3E• 24. 36 K = 5.620 P = 22.84 1 3 C =120 0.00 0.00 1.52 Q= 70.0 IN 1. 380" 70.0 0.3474 14.29 4.96 22.84 29.6 1.610 OE 4.0 10.17 29.32 29. 32 K = 5.620 P = 27. E.E. 1 4 C=120 1T .8.0 8.00 0.00 1. E.E. Q= 99.6 IN 1.610" 3.3. E, 0. 314.3 18.17 5. 72 27. 66 39. E, 35.04 K 2= 16.83 1 -T 99.6 2.157 15.00 35.9E, QA= 99. E. PT= 35.9E CM C=120 0.00 0.00 99.6' 0.0757 15.00 1.14 99.6 2.157 42.58 37.10 37.10 K= 16.830 P= 35.04 cm C=120 31.00 0.00 2.06 Q= 199.2 IN 2.157" 199.2 0.2732 31.00FT 73.58 20.10 35.04 199.2 57.20 K 3= 26.34 199.2 4.026 0.00 57.20 QA= 199.2 PT= 57.20 STDP C=120 0.00 0.00 199.2 0.0130 0.00 0.00 500.0 4.026 72.00 57.20 QA= 500.0 PT= 57.20 STDP C =120 0.00 32.30 Q = E- 3'3.2 IN 4.026" 699.2 0.1334 72.00 9.61 PE=. 4331 X 74. 57 ` 699.2 99.11 K 4= 70.23 STDP 699.2 8.071 0.00 99.11 GA = 699.2 P T = 99.11 UDG C=120 0.00 0.00 E-39.2 0.0045 0.00 0.00 250.0 8.071 42.00 99.11, QA= 250.0 PT= 99.11 UDG C=120 100.00 0.00 (3= 949.2 IN 8.071" 949.2 0.0079 100.00FT 142.00 1.13 W I lGI "TON F= I FRE SP F:Z I "lKL_EFRS e.JOB— JOB JOB NO DATE PAGE 2 t DESIGN AREA #2tt## I HYDRLC. GA DIA. EGUIV. PIPE PT PT REF. FLOW "C" FITTING FTGS. PE PV ##### NOTES ## POINT GT LOSS/FT LENGTHS TOT. PF PN 949. 2 100.24 K 5= 94.81 UDG 41 i DENSITY X AREA 0.100 X 1500.0 = 150.00 OVERAGE = 79.00 GPM = 79.00 RACKS = 0.00 INSIDE HOSES - 750.00 OUTSIDE HOSES = 0.00 FLOW REG`D FOR SYSTEM = 229.00 FLOW AT BASE OF RISER = 979.00 MIN FLOW AT BASE OF RISER = 979.00 TOTAL FLOW = 979.00 STATIC PRESSURE = 60.00 RESIDUAL PRESSURE = 40.00 RESIDUAL FLOW = 979.00 FLOW FROM CITY SUPPLY AT 20PSI = 1424 GPM PUMP RATING 75.00 PSI AT 750.00 GPM PRESSURE FROM CURVE @ TOTAL FLOW - 100.45 ELEVATION = 2..50 FT = 1.08 NO. DIA "C" LENGTH FACTOR + FLOW PF FLOW ADDITIONAL VALVE LOSS, ETC. - 0.00 SAFETY MARGIN (IN PSI) = 0.00 PRESSURE AVAILABLE FOR SYSTEM = 101.53 i i i i DENSITY X AREA 0.100 X 1500.0 = 150.00 OVERAGE = 79.00 GPM 79.00 RACKS = 0.00 INSIDE HOSES = 750.00 OUTSIDE HOSES = 0.00 FLOW REG'D FOR SYSTEM = 229.00 FLOW AT BASE OF RISER = 979.00 MIN FLOW AT BASE OF RISER = 979.00 TOTAL FLOW = 979.00 STATIC PRESSURE = E.0.00 RESIDUAL PRESSURE = 40.00 RESIDUAL FLOW = 1060.00 FLOW FROM CITY SUPPLY AT 20PSI = 1542 GPM PRESSURE FROM CURVE to TOTAL FLOW = 42.79 ELEVATION = 0.00 FT = 0.00 NO. DIA "C" LENGTH FACTOR + FLOW PF FLOW 1 7.980 140 408.00 G IH 0.0 2.73 979.00 ADDITIONAL VALVE LOSS, ETC. = 0.00 SAFETY MARGIN (IN PSI) = 0.00 PRESSURE AVAILABLE FOR SYSTEM = 40.00 i 4 VI-\\/L