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| author | prashantsinalkar | 2017-10-10 12:27:19 +0530 |
|---|---|---|
| committer | prashantsinalkar | 2017-10-10 12:27:19 +0530 |
| commit | 7f60ea012dd2524dae921a2a35adbf7ef21f2bb6 (patch) | |
| tree | dbb9e3ddb5fc829e7c5c7e6be99b2c4ba356132c /3685/CH14/EX14.4/Ex14_4.sce | |
| parent | b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (diff) | |
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initial commit / add all books
Diffstat (limited to '3685/CH14/EX14.4/Ex14_4.sce')
| -rw-r--r-- | 3685/CH14/EX14.4/Ex14_4.sce | 32 |
1 files changed, 32 insertions, 0 deletions
diff --git a/3685/CH14/EX14.4/Ex14_4.sce b/3685/CH14/EX14.4/Ex14_4.sce new file mode 100644 index 000000000..8c308aebd --- /dev/null +++ b/3685/CH14/EX14.4/Ex14_4.sce @@ -0,0 +1,32 @@ +clc
+h3 = 882 // Enthalpy at state 3 in kJ/kg
+h2 = 1034 // Enthalpy at state 2 in kJ/kg
+h6 = 998 // Enthalpy at state 6 in kJ/kg
+h1 = 1008 // Enthalpy at state 1 in kJ/kg
+v1 = 0.084 // Specific volume at state 1 in m^3/kg
+t4 = 25 // Temperature at state 4 in degree Celsius
+m = 10 // mass flow rate in kg/s
+h4 = h3-h1+h6
+h5 = h4 // isenthalpic process
+w = (m*14000)/((h6-h5)*3600) // in kg/s
+VFR = w*3600*v1 // Volume flow rate in m^3/h
+ve = 0.8 // volumetric efficiency
+CD = VFR/(ve*60) // Compressor displacement in m^3/min
+N = 900 // Number of strokes per minute
+n = 2 // number of cylinder
+
+D = ((CD*4)/(%pi*1.1*N*n))^(1/3) // L = 1.1D L = length D = diameter
+L = 1.1*D
+COP = (h6-h5)/(h2-h1) // coefficient of performance
+PI = w*(h2-h1) // Power input
+
+printf("\n Example 14.4\n")
+printf("\n Refrigeration effect is %d kJ/kg",h6-h5)
+printf("\n Refrigerant flow rate is %f kg/s",w)
+printf("\n Diameter of cylinder is %f cm",D*100)
+printf("\n Length of cylinder is %f cm",L*100)
+printf("\n COP is %f ",COP)
+printf("\n Power required to drive the compressor is %f kW",PI)
+
+//The answers vary due to round off error
+
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