CENTRIFUGAL PUMPCLIENT EQUIP. NO PAGE

REV PREPARED BY DATE APPROVAL W.O. REQUISITION NO. SPECIFICATION NO.

0 1 UNIT AREA PROCURED BY INSTALLED BY2

name of pump goes here1 General2 Fluid Service Mother Liquor Pump Manufacturer Goulds3 Number Required one Model Number 3196STD4 Pump Type ANSI AA Back Pullout Size 1 x 1-1/2 x 85 Location Indoor6 Process Data7 Fluid Pumped Mother Liquor8 Normal Flow Rate gpm 50.0 Corrosive or Non-Corrosive non-corrosive9 Design Flow Rate gpm 50.0 Corrosive Compounds n/a10 Pumping Temperature deg F 95.0 Solids none11 Vapor Pressure @ P.T. psia 0.5 12 Viscosity @ P.T. cP 2.1 Hazards13 Specific Gravity @ P.T. water=1 1.1 14 Pumping Conditions15 Suction Discharge 16 Terminal Pressure psia 14.7 14.7 17 Static Head ft / psi 2.0 1.0 20.0 9.9 18 Equipment Loss (see sketch) ft / psi - - - - 19 Line Loss (per 100 equiv ft) ft / psi 6.6 3.3 24.3 12.0 20 Equiv. Line Length ft 8 38021 Safety Factor in Line Loss (%) 0% 20%22 Total friction Loss ft / psi 0.5 0.3 111.0 54.8 23 Control Valve ft / psi - - - - 24 Net Suction Pressure psia 15.4 25 NPSH available ft / psia 39.3 14.9 26 Total Discharge Pressure psia 79.4 27 Differential Pressure (TDH) ft / psi 168.4 63.9 28 Design Flow Rate gpm 50.0 2930 Mechanical Data31 Type Material Sketch32 Pump Head mfg std 316SS33 Impeller 6-1/2" diam. 316SS34 Shaft less sleeve 316SS35 Seal Mechanical carbon vs ceramic36 Baseplate fabricated steel3738 Connections Suction 1-1/2" ANSI RF Case Drn.39 Discharge 1" ANSI RF40 Electrical Data41 Area Classification Class 1 Group D Division 2 Enclosure TEFC42 Power Volts 460 Phases 3 Cycles 60 Frame 145T43 Horsepower Calculated 1.86 BHP 3.33 Nominal 5.0 RPM 175044 Efficiency 56%45 Notes46474849505152

CENTRIFUGAL PUMPCLIENT EQUIP. NO PAGE

REV PREPARED BY DATE APPROVAL W.O. REQUISITION NO. SPECIFICATION NO.

0 1 UNIT AREA PROCURED BY INSTALLED BY2

name of pump goes here1 General2 Fluid Service Mother Liquor Pump Manufacturer Goulds3 Number Required one Model Number 3196STD4 Pump Type ANSI AA Back Pullout Size 1 x 1-1/2 x 85 Location Indoor6 Process Data7 Fluid Pumped Mother Liquor8 Normal Flow Rate gpm 50.0 Corrosive or Non-Corrosive non-corrosive9 Design Flow Rate gpm 50.0 Corrosive Compounds n/a

10 Pumping Temperature deg F 95.0 Solids none11 Vapor Pressure @ P.T. psia 0.5 12 Viscosity @ P.T. cP 2.1 Viscosity cSt 1.8 13 Specific Gravity @ P.T. water=1 1.1 SSU 8.6 14 Data From Published Curve for Selected Pump15 Point 1 Point 2 At Best Point 416 Eff Pt.17 Flow Rate on Curve (gpm) 450.0 600.0 750.0 900.0 18 Corresponding Head (ft. liquid) 114.0 108.0 100.0 86.0 19 Corresponding Efficiency (%) 72.5% 80.0% 82.0% 79.5%202122 Pump Performance with Viscous Fluid23 Point 1 Point 2 At Best Point 424 Eff Pt.25 Viscous Flow Rate 450.0 600.0 750.0 900.0 26 Viscous Head 114.0 108.0 100.0 86.0 27 Viscous Efficiency 72.5% 80.0% 82.0% 79.5%28 Viscous bhp 20.4 23.3 26.3 28.0 293031323334353637383940414243444546474849 Reference: Sorrell, T., Taylor, R.P., Hodge, B.K., "Estimating Pump50 Curves for High-Viscosity Fluids", Heating/Piping/Air51 Conditioning, October 1990, p.7552

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Pump Performance with Viscous Fluid

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