From b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b Mon Sep 17 00:00:00 2001
From: priyanka
Date: Wed, 24 Jun 2015 15:03:17 +0530
Subject: initial commit / add all books

---
 2969/CH2/EX2.1/Ex2_1.sce | 24 ++++++++++++++++++++++++
 2969/CH2/EX2.2/Ex2_2.sce | 27 +++++++++++++++++++++++++++
 2 files changed, 51 insertions(+)
 create mode 100755 2969/CH2/EX2.1/Ex2_1.sce
 create mode 100755 2969/CH2/EX2.2/Ex2_2.sce

(limited to '2969/CH2')

diff --git a/2969/CH2/EX2.1/Ex2_1.sce b/2969/CH2/EX2.1/Ex2_1.sce
new file mode 100755
index 000000000..73952824f
--- /dev/null
+++ b/2969/CH2/EX2.1/Ex2_1.sce
@@ -0,0 +1,24 @@
+clc
+clear
+//DATA GIVEN
+c=88;                   //% of carbon in coal
+h=4.2;                  //% of hydrogen in coal
+Wf=0.848;               //weight of coal in g
+Wfw=0.027;              //weight of fuse wire in calorimeter in g
+W=1950;                 //weight of water in calorimeter in g
+We=380;                 //water equivalent of calorimeter
+Dt=3.06;                //observed temperature rise (t2-t1) in deg celsius
+tc=0.017;               //cooling correction in deg celsius
+cfw=6700;               //calorific value of fuse wire in J/g
+
+//CALCULATIONS
+ctr=(Dt)+tc;            //corrected temp. rise
+Hw=(W+We)*4.18*[ctr];   //heat recieved by water in J
+Hfw=Wfw*cfw;            //heat given out by fuse wire in J
+Hcf=Hw-Hfw;             //heat produced due to combustion of fuel in J
+HCV=Hcf/Wf;             //higher calorific value of fuel in kJ/kg
+Ms=9*h/100;             //steam produced per kg of coal
+LCV=HCV-2465*Ms;        //lower calorific value of fuel in kJ/kg
+
+printf('The Higher calorific value of fuel, H.C.V. is: %5.1f kJ/kg. \n',HCV);
+printf(' The Lower calorific value of fuel, L.C.V. is: %5.1f kJ/kg. \n',LCV);
diff --git a/2969/CH2/EX2.2/Ex2_2.sce b/2969/CH2/EX2.2/Ex2_2.sce
new file mode 100755
index 000000000..a06563e31
--- /dev/null
+++ b/2969/CH2/EX2.2/Ex2_2.sce
@@ -0,0 +1,27 @@
+clc
+clear
+//DATA GIVEN
+V1=0.08;                 //gas burnt in calorimeter in m^3
+Pg=5.2;                  //pressure of gas supply in cm of water
+Pb=75.5;                 //barometer reading in cm of Hg
+Ww=28;                   //weight of water heated by gas in kg
+Tg=13;                   //temperature of gas in deg celsius
+Twi=10;                  //temperature of water at inlet in deg celsius
+Two=23.5;                //temperature of water at outlet in deg celsius
+Ms=0.06;                 //steam condensed in kg
+
+//CALCULATIONS
+//by using general gas equation, reducing the volume to S.T.P.
+//p1*V1/T1=p2*V2/T2
+p1=Pb+(Pg/13.6);         //in cm of Hg
+T1=Tg+273;               //in K
+p2=76;                   //in cm of Hg
+T2=15+273;               //in K
+V2=p1*V1*T2/T1/p2;       //in m^3
+Hw=Ww*4.18*(Two-Twi);    //heat recieved by water in kJ
+HCV=Hw/V1;               //higher calorific value of fuel in kJ/m^3
+LCV=HCV-2465*Ms/V1;      //lower calorific value of fuel in kJ/m^3
+
+printf(' The Calorific values of fuel per m^3 of gas at 15 deg celsius and 76 cm of Hg pressure are: \n');
+printf('  The Higher calorific value of fuel, H.C.V. is: %5.1f kJ/m^3. \n',HCV);
+printf('  The Lower calorific value of fuel, L.C.V. is: %5.1f kJ/m^3. \n',LCV);
-- 
cgit