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In accordance to ASME PTC10 (1997) page 123 onwards
Design conditions
Inlet Discharge
Pressure (barA) 2.878 6.303 U2_1st impeller (m/s) = 202.61
Temperature (deg. C) 15 93 Machine Mach number = 0.8102
Specific volume (m^3/kg) 0.1610 0.0934 Machine Reynolds number = 3428517
Zed 0.9870 0.9871 Pressure ratio = 2.19006
Viscosity (kg/m.s) 7.60E-06 9.63E-06
Cp (J/kg.K) 639.09 658.51 Volume ratio = 1.72330
Cp/Cv 1.3694 1.3581
Sonic velocity (m/s) 250.06 279.68 RC = 0.02551
Enthalpy (J/kg) 166575 215381 RB = -8.95578
Entropy (J/kg.K) 2972436 2996205 RA = 0.66000
Polytropic efficiency = 0.841 nv1 = 1.446504533
Polytropic head (J/kg) = 41054 nv2 = 1.420464911
Molecular weight (kg/kmol) = 51.04 nt1 = 1.449619552
Rotational speed (rpm) = 13117 nt2 = 1.436549887
Max. design Temp. (deg. C) = 180 nv_avg = 1.433484722
1st critical speed (rpm) = 7506 nt_avg = 1.44308472
2nd critical speed (rpm) = 16617
1st imp. 2nd imp. 3rd imp. 4th imp. 5th imp. 6th imp. 7th imp. 8th imp. 9th imp. 10th imp.
Diameter (m) 0.295 0.294 na na na na na na na na
Tip width (m) 0.0207 0.0163 na na na na na na na na
Test conditions
Gas = 100% CO2
Suction pressure (barA) = 3.5
Suction temperature (deg. C) = 25 T2_calc (deg. C) 82.56549827
Molecular weight (kg/kmol) = 44.01 Hp (J/kg) 41055.93
Zed_1 = 0.981895011 Rem_corr_guess 0.999953089
Specific volume (m^3/kg) = 0.158021840 Poly. eff_guess 0.841039454
Speed (rpm) 13117.0000
Zed_2 0.980961232
Viscosity (kg/m.s) = 8.2981E-06 V_2 (m^3/kg) 0.095762958
nv1 = 1.3643437901 Volume ratio 1.650135332
nt1 = 1.3656319941 Schultz factor, f 1.004850748
1st impeller U2 (m/s) 202.61
Reynolds number 3198381
Remt/Remsp 0.932876034
RC 0.025945312
RB -8.953562012
RA 0.660000406
Poly. eff_calc 0.841039454
Rem_corr_calc 0.999953089
T2_guess (deg. C) 82.56549827
P2_input (barA) 6.884023950
nv2 1.326556040
nt2 1.340639124
nv_avg 1.345449915
nt_avg 1.353135559

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CL2 compression SOP report_26 May 2016
 

LP_point_6_(LtR)

  • 1. In accordance to ASME PTC10 (1997) page 123 onwards Design conditions Inlet Discharge Pressure (barA) 2.878 6.303 U2_1st impeller (m/s) = 202.61 Temperature (deg. C) 15 93 Machine Mach number = 0.8102 Specific volume (m^3/kg) 0.1610 0.0934 Machine Reynolds number = 3428517 Zed 0.9870 0.9871 Pressure ratio = 2.19006 Viscosity (kg/m.s) 7.60E-06 9.63E-06 Cp (J/kg.K) 639.09 658.51 Volume ratio = 1.72330 Cp/Cv 1.3694 1.3581 Sonic velocity (m/s) 250.06 279.68 RC = 0.02551 Enthalpy (J/kg) 166575 215381 RB = -8.95578 Entropy (J/kg.K) 2972436 2996205 RA = 0.66000 Polytropic efficiency = 0.841 nv1 = 1.446504533 Polytropic head (J/kg) = 41054 nv2 = 1.420464911 Molecular weight (kg/kmol) = 51.04 nt1 = 1.449619552 Rotational speed (rpm) = 13117 nt2 = 1.436549887 Max. design Temp. (deg. C) = 180 nv_avg = 1.433484722 1st critical speed (rpm) = 7506 nt_avg = 1.44308472 2nd critical speed (rpm) = 16617 1st imp. 2nd imp. 3rd imp. 4th imp. 5th imp. 6th imp. 7th imp. 8th imp. 9th imp. 10th imp. Diameter (m) 0.295 0.294 na na na na na na na na Tip width (m) 0.0207 0.0163 na na na na na na na na Test conditions Gas = 100% CO2 Suction pressure (barA) = 3.5 Suction temperature (deg. C) = 25 T2_calc (deg. C) 82.56549827 Molecular weight (kg/kmol) = 44.01 Hp (J/kg) 41055.93 Zed_1 = 0.981895011 Rem_corr_guess 0.999953089 Specific volume (m^3/kg) = 0.158021840 Poly. eff_guess 0.841039454 Speed (rpm) 13117.0000 Zed_2 0.980961232 Viscosity (kg/m.s) = 8.2981E-06 V_2 (m^3/kg) 0.095762958 nv1 = 1.3643437901 Volume ratio 1.650135332 nt1 = 1.3656319941 Schultz factor, f 1.004850748 1st impeller U2 (m/s) 202.61 Reynolds number 3198381 Remt/Remsp 0.932876034 RC 0.025945312 RB -8.953562012 RA 0.660000406 Poly. eff_calc 0.841039454 Rem_corr_calc 0.999953089 T2_guess (deg. C) 82.56549827 P2_input (barA) 6.884023950 nv2 1.326556040 nt2 1.340639124 nv_avg 1.345449915 nt_avg 1.353135559