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• is Calculation No. 145579-V-CA-004 Rev. No.1 Calculation Title O ff-Gas Chiller Ca lculation Because q:oifull>gtottri 2. Equipment Selection RPP-24544 REV ]d CALCULATION SHEET glotyi = 17.58Tonn gtotfull . 3225Tonn qrequired := glolfull qrequired = 3225Tonn Originator Date:"? °s Checker. Date: O'( IykV 0 York air cooled scroll chiller will be selected to cool p ropylene glycoVwater 50% by weight solution, with freezing point of -25 F. Selection: Type: YCAL0042EC Rated Capacity. 40.8 Tonn Input Power. 57 kW Equipment selec ti on, performance data and correc ti on factors a re per "York Inte rnational- Form 150.62-E61 'Selection Data' -Capacity Correction for Proplyene: Qrated:= 40.8Tonn Pinput:' 57kW Efficiency. Eff = ON Eff ^. 0.928 (50"1") KW Q:= Qraad•Eff Q=37.86Tonn Input Power. KW :- qrt Q P• mput' Eff Q -Flow Through Chiller (Coo li ng Fluid) KW = 45.06kW GPM formula: (Ref 2) grequimd' GF GPM z AT GPM FITON Factor. (Ref 2) PI . R GF:= 272 min Tonn Page 4 • Temperatu re Range: (Assumption 6) &T:= I OR Temperature range is selected as sugested, with enginee ri ng judgement (as being most common and efficient), by "York A5-643
0 NisE Calculation No. 145579-V-CA-004 Rev. No.1 Calculation Title Off-Gas Chiller Calculation 3. Pump Selection Calculation RPP-24544 REV Id CALCULATION SHEET Origlnatoc D ate: 7r^ yyb!>1 ^(x'05 Checker: A Date: 0.1 t-t brit, 05 grequired'OF Intemationar'Selection Data'. GPM :_ AT GPM = 87.73 gal min OH-Gas Chiller Calculation (145579-V-CA- 004) to be Revised 3.1 PROPLYENE GLYCOL PRESSURE DROP CORRECTION FACTOR 50% by weight mixtu re Cooler Pressu re Drop Correc ti on Factor for P ropyene Glyco l/Water. • (Data Sheet 145579-V-DS-12.1, Appendix A, Page l 1 of 116.) 3.2 EQUIPMENT PRESSURE LOSS 32.1 Cooler Pressu re Drop Flow Rate: (From Section 2 of this calculation) Pressu re Drop: (From Cooler Cu rves, Pg 14 of 114) Cooler Pressure Drop (factored): APf := 1.247 GPM - 87.73 gal min AP := 6.5ftI120 32.2 Scrubber #1- Heat Exchanger P ressu re Drop Scrubber Pressu re Drop: AP-- 5psi (Assumption 3) Heat Exchanger P ressu re Drop: APh ex = AP•APf (Conse rvative Approach,eonected - for propyene glyco l) 3.3 PIPING AND VALVES V2 Head Loss: AHI 5 k. • (ASHRAE Fundamentals) 2.8 Table 2 - K factors for welded pipe fittings: (2001 ASHRAE Fundamentals Handbook) Pipe Diameter. Dx 3in AFcooler = AP'APf APeoo1R = 8.11=0 A5-644 AP- 11.54 11112O Aphex ° 1439ftH2O Page 5 of 6
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