diff options
author | priyanka | 2015-06-24 15:03:17 +0530 |
---|---|---|
committer | priyanka | 2015-06-24 15:03:17 +0530 |
commit | b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (patch) | |
tree | ab291cffc65280e58ac82470ba63fbcca7805165 /527/CH2/EX2.18 | |
download | Scilab-TBC-Uploads-b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b.tar.gz Scilab-TBC-Uploads-b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b.tar.bz2 Scilab-TBC-Uploads-b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b.zip |
initial commit / add all books
Diffstat (limited to '527/CH2/EX2.18')
-rwxr-xr-x | 527/CH2/EX2.18/2_18exam.sce | 13 |
1 files changed, 13 insertions, 0 deletions
diff --git a/527/CH2/EX2.18/2_18exam.sce b/527/CH2/EX2.18/2_18exam.sce new file mode 100755 index 000000000..434933064 --- /dev/null +++ b/527/CH2/EX2.18/2_18exam.sce @@ -0,0 +1,13 @@ +//Engineering and Chemical Thermodynamics
+//Example 2.18
+//Page no :84
+
+clear ; clc ;
+m_dot_1 = 10 ; //[kg/s]
+h_cap_1 = 3238.2 ;//[kJ/kg], Super heated steam at 500*C & 200bar
+h_cap_2 = 93.3 ;//[kL/kg], subcooled liquid at 20*C & 100bar
+h_cap_3 = 2724.7 ;//{kJ/kg}, Super heated vapour at 100bar
+
+m_dot_2 = m_dot_1 * (h_cap_1 - h_cap_3) / (h_cap_3 - h_cap_2);
+disp(" Example: 2.18 Page no : 84") ;
+printf('\n Flow of liquid stream = %.2f kg/s',m_dot_2);
\ No newline at end of file |