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authorpriyanka2015-06-24 15:03:17 +0530
committerpriyanka2015-06-24 15:03:17 +0530
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-rwxr-xr-x2510/CH21/EX21.1/Ex21_1.sce22
-rwxr-xr-x2510/CH21/EX21.2/Ex21_2.sce16
-rwxr-xr-x2510/CH21/EX21.3/Ex21_3.sce16
3 files changed, 54 insertions, 0 deletions
diff --git a/2510/CH21/EX21.1/Ex21_1.sce b/2510/CH21/EX21.1/Ex21_1.sce
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index 000000000..d8d30f789
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@@ -0,0 +1,22 @@
+//Variable declaration:
+m = 1 //Mass flowrate (lb)
+cP = 1 //Heat capacity (Btu/lb. F)
+//From figure 21.3:
+T1 = 300 //Temperature of hot fluid leaving exchanger ( F)
+T2 = 540 //Temperature of hot fluid entering exchanger ( F)
+T3 = 60 //Temperature of cold fluid leaving exchanger ( F)
+T4 = 300 //Temperature of cold fluid entering exchanger ( F)
+
+//Calculation:
+DSh = m*cP*log((T1+460)/(T2+460)) //Entropy for hot fluid (Btu/ F)
+DSc = m*cP*log((T4+460)/(T3+460)) //Entropy for cold fluid (Btu/ F)
+DSa = DSh+DSc //Entropy for one exchanger (Btu/ F)
+DSt = DSa*2 //Total entropy change (Btu/ F)
+
+//Result:
+printf("The entropy chage is : %.4f Btu/ F .",DSt)
+if (DSt>0) then
+ printf("There is a positive entropy change.")
+else
+ printf("There is a negative entropy change.")
+end
diff --git a/2510/CH21/EX21.2/Ex21_2.sce b/2510/CH21/EX21.2/Ex21_2.sce
new file mode 100755
index 000000000..f5b06ae38
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+//Variable declaration:
+//From example 21.1:
+DSh = -0.2744 //Entropy for hot fluid (Btu/ F)
+DSc = 0.3795 //Entropy for cold fluid (Btu/ F)
+m = 1 //Mass flowrate (lb)
+cP = 1 //Heat capacity (Btu/lb. F)
+//From figure 21.4:
+DT = 0 //Temperature difference driving force ( F)
+DS_D = 0 //Entropy for D exchanger (Btu/ F)
+
+//Calculation:
+DS_C = DSh+DSc //Entropy for C exchanger (Btu/ F)
+DSt = DS_C+DS_D //Total entropy change of exchangers (Btu/ F)
+
+//Result:
+printf("The total entropy change is : %f Btu/ F .",DSt)
diff --git a/2510/CH21/EX21.3/Ex21_3.sce b/2510/CH21/EX21.3/Ex21_3.sce
new file mode 100755
index 000000000..a340e8add
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+++ b/2510/CH21/EX21.3/Ex21_3.sce
@@ -0,0 +1,16 @@
+//Variable declaration:
+//From figure 21.5:
+m = 2 //Mass flowrate (lb)
+cP = 1 //Heat capacity (Btu/lb. F)
+DS1 = -0.2744 //Entropy for hot fluid for E exchanger (Btu/ F)
+T1 = 180 //Temperature cold fluid entering the E exchabger ( F)
+T2 = 60 //Temperature cold fluid leaving the E exchabger ( F)
+
+//Calculation:
+DS2 = m*cP*log((T1+460)/(T2+460)) //Entropy for cold fluid for E exchanger (Btu/ F)
+DS_E = DS1+DS2 //Entropy for E exchanger (Btu/ F)
+DS_F = DS_E //Entropy for F exchanger (Btu/ F)
+DSt = DS_F+DS_E //Entropy change in exchangers E and F (Btu/ F)
+
+//Result:
+printf("The entropy change in exchangers E and F is : %.4f Btu/ F",DSt)