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Diffstat (limited to '409/CH19/EX19.1/Example19_1.sce')
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diff --git a/409/CH19/EX19.1/Example19_1.sce b/409/CH19/EX19.1/Example19_1.sce new file mode 100755 index 000000000..7c7d5cabd --- /dev/null +++ b/409/CH19/EX19.1/Example19_1.sce @@ -0,0 +1,35 @@ +clear ; +clc; +// Example 19.1 +printf('Example 19.1\n\n'); +//Page No. 563 +// Solution + +// Use phase rule to get degree of freedom(F) = 2-P+C +// (a) +N1 = 1; +P1 = 1 ;// Number of phases present +C1 = 1 ;//Number of components present +F1 = 2-P1+C1 ;//Number of degree of freedom +printf('\n (a) Number of degree of freedom of pure benzene is %i. Therefore %i additional intensive variables must be specified to fix the system.\n ',F1,F1); + +// (b) +N2 = 1; +P2 = 2 ;// Number of phases present +C2 = 1 ;//Number of components present +F2 = 2-P2+C2 ;//Number of degree of freedom +printf('(b) Number of degree of freedom of a mixture of ice and water only is %i. Therefore %i additional intensive variables must be specified to fix the system.\n ',F2,F2); + +// (c) +N3 = 2; +P3 = 2 ;// Number of phases present +C3 = 2 ;//Number of components present +F3 = 2-P3+C3 ;//Number of degree of freedom +printf('(c) Number of degree of freedom of a mixture of liquid benzene,benzene vapour and helium gas is %i. Therefore %i additional intensive variables must be specified to fix the system.\n ',F3,F3); + +// (d) +N4 = 2; +P4 = 2 ;// Number of phases present +C4 = 2 ;//Number of components present +F4 = 2-P4+C4 ;//Number of degree of freedom +printf('(d) Number of degree of freedom of a mixture of salt and water designed to achieve a specific vapour pressure is %i. Therefore %i additional intensive variables must be specified to fix the system.\n ',F4,F4);
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