From ceb2aae7af9263016f51c0a073a9233922e9ac3d Mon Sep 17 00:00:00 2001
From: prashantsinalkar
Date: Tue, 5 Mar 2019 12:22:19 +0530
Subject: updated the code for scilab on cloud[scilab 5.5.2]

---
 905/CH8/EX8.3/8_3.sce | 86 +++++++++++++++++++++++++--------------------------
 1 file changed, 43 insertions(+), 43 deletions(-)

diff --git a/905/CH8/EX8.3/8_3.sce b/905/CH8/EX8.3/8_3.sce
index 63c1bbace..412c1ba2e 100755
--- a/905/CH8/EX8.3/8_3.sce
+++ b/905/CH8/EX8.3/8_3.sce
@@ -1,44 +1,44 @@
-clear;
-clc;
-
-// Illustration 8.2
-// Page: 482
-
-printf('Illustration 8.3 -  Page: 482\n\n');
-
-// solution
-// A - water vapor   B - air
-//*****Data*****
-T = 328; // [dry bulb temperature, K]
-P_total = 1; // [atm]
-H = 30; // [relative humidity, %]
-//*****//
-P_vapA = 15.73; // [vapor pressure of water, kPa]
-P_total = P_total*101.325; // [kPa]
-M_A = 18; // [gram/mole]
-M_B = 29; // [gram/mole]
-
-P_A = (H/100)*P_vapA;// [partial pressure of A,kPa]
-
-printf('Illustration 8.3 (a)\n\n');
-// At dew point partial pressure is equal to vapor pressure
-// Using Antonnie equation we can find dew point temperature
-
-printf("Dew point temperature is 304.5 K\n")
-
-// From equation 8.1
-Y_s = P_A/(P_total-P_A)*(M_A/M_B);
-printf("Absolute humidity of air-water mixture at 328 K is %f kg H2O/kg dry air\n\n",Y_s);
-
-printf('Illustration 8.3 (b)\n\n');
-
-//soluton (b)
-T_ref = 273; // [K]
-C_A = 1.884; // [kJ/kg.K]
-C_B = 1.005; // [kJ/kg.K]
-lambda = 2502.3; // [Latent heat of Vaporization at 273 K, kJ/kg]
-
-// From equation 8.3
-H_s = C_B*(T-T_ref) + Y_s*(C_A*(T-T_ref) + lambda);
-
+clear;
+clc;
+
+// Illustration 8.3
+// Page: 482
+
+printf('Illustration 8.3 -  Page: 482\n\n');
+
+// solution
+// A - water vapor   B - air
+//*****Data*****
+T = 328; // [dry bulb temperature, K]
+P_total = 1; // [atm]
+H = 30; // [relative humidity, %]
+//*****//
+P_vapA = 15.73; // [vapor pressure of water, kPa]
+P_total = P_total*101.325; // [kPa]
+M_A = 18; // [gram/mole]
+M_B = 29; // [gram/mole]
+
+P_A = (H/100)*P_vapA;// [partial pressure of A,kPa]
+
+printf('Illustration 8.3 (a)\n\n');
+// At dew point partial pressure is equal to vapor pressure
+// Using Antonnie equation we can find dew point temperature
+
+printf("Dew point temperature is 304.5 K\n")
+
+// From equation 8.1
+Y_s = P_A/(P_total-P_A)*(M_A/M_B);
+printf("Absolute humidity of air-water mixture at 328 K is %f kg H2O/kg dry air\n\n",Y_s);
+
+printf('Illustration 8.3 (b)\n\n');
+
+//soluton (b)
+T_ref = 273; // [K]
+C_A = 1.884; // [kJ/kg.K]
+C_B = 1.005; // [kJ/kg.K]
+lambda = 2502.3; // [Latent heat of Vaporization at 273 K, kJ/kg]
+
+// From equation 8.3
+H_s = C_B*(T-T_ref) + Y_s*(C_A*(T-T_ref) + lambda);
+
 printf("Enthalpy per unit mass of dry air of a saturated mixture relative to 273 K is %f kJ/kg dry air\n",H_s);
\ No newline at end of file
-- 
cgit