diff options
Diffstat (limited to '1943/CH5')
-rwxr-xr-x | 1943/CH5/EX5.1/Ex5_1.sce | 14 | ||||
-rwxr-xr-x | 1943/CH5/EX5.2/Ex5_2.sce | 21 | ||||
-rwxr-xr-x | 1943/CH5/EX5.3/Ex5_3.sce | 24 | ||||
-rwxr-xr-x | 1943/CH5/EX5.4/Ex5_4.sce | 22 | ||||
-rwxr-xr-x | 1943/CH5/EX5.5/Ex5_5.sce | 20 | ||||
-rwxr-xr-x | 1943/CH5/EX5.6/Ex5_6.sce | 22 |
6 files changed, 123 insertions, 0 deletions
diff --git a/1943/CH5/EX5.1/Ex5_1.sce b/1943/CH5/EX5.1/Ex5_1.sce new file mode 100755 index 000000000..8caf9211e --- /dev/null +++ b/1943/CH5/EX5.1/Ex5_1.sce @@ -0,0 +1,14 @@ + +clc
+clear
+//Input data
+Vs=2500;//The mass of a bed of solid particles in kg
+p=2650;//The density of the solid in kg/m^3
+d=800*10^-6;//The mean particle size in m
+s=0.84;//The sphericity of the particle
+
+//Calculations
+As=(6*Vs)/(p*d*s);//The total surface area of the particles in the bed
+
+//Output
+printf(' The total surface area of the particles in the bed As = %3.0f m^2 ',As)
diff --git a/1943/CH5/EX5.2/Ex5_2.sce b/1943/CH5/EX5.2/Ex5_2.sce new file mode 100755 index 000000000..c04c4f6dd --- /dev/null +++ b/1943/CH5/EX5.2/Ex5_2.sce @@ -0,0 +1,21 @@ + +clc
+clear
+//Input data
+d=427*10^-6;//The mean particle size in m
+pg=1.21;//The density of air in kg/m^3
+v=1.82*10^-5;//The viscosity of air in kg/ms
+pl=1620;//The density of the loosely packed bed in kg/m^3
+ps=2780;//The density of the solids in kg/m^3
+c1=27.2;//(Grace,1982)constant value.
+c2=0.0408;//(Grace,1982)constant value
+g=9.812;//Gravitational forc constant in m/s^2
+
+//Calculations
+E=1-(pl/ps);//The voidage of the bed
+Ar=[(pg)*(ps-pg)*g*(d^3)]/v^2;//Archimedes number
+Re=[c1^2+(c2*Ar)]^(0.5)-c1;//Reynolds number
+Umf=Re*v/(pg*d);//Minimum superficial velocity in m/s
+
+//Output
+printf('(a) The voidage of the bed = %3.3f \n (b) The minimum fluidization velocity Umf = %3.3f m/s ',E,Umf)
diff --git a/1943/CH5/EX5.3/Ex5_3.sce b/1943/CH5/EX5.3/Ex5_3.sce new file mode 100755 index 000000000..52d1b6f52 --- /dev/null +++ b/1943/CH5/EX5.3/Ex5_3.sce @@ -0,0 +1,24 @@ + +clc
+clear
+//Input data
+d=427*10^-6;//The mean particle size in m
+pg=1.21;//The density of air in kg/m^3
+v=1.82*10^-5;//The viscosity of air in kg/ms
+Umf=0.14;//Minimum superficial velocity in m/s
+Ar=7753;//Archimedes number from previous example problem
+
+//Calculations
+Re=(Umf*pg*d)/v;//Reynolds number
+function[f] = F(x);//function definition
+ f = 7753*x^2- 381.1*x -4793;
+endfunction
+x = 100;//Initial guss
+function[z] = D(x)//Derivative
+ z= 3*x^2 - 3;
+endfunction
+y = fsolve(x,F, D);
+
+//Output
+printf('The sphericity of particles is = %3.3f ',y)
+
diff --git a/1943/CH5/EX5.4/Ex5_4.sce b/1943/CH5/EX5.4/Ex5_4.sce new file mode 100755 index 000000000..be366b709 --- /dev/null +++ b/1943/CH5/EX5.4/Ex5_4.sce @@ -0,0 +1,22 @@ + +clc
+clear
+//Input data
+O=35;//The output of the fluidized bed combustion system in MW
+n=0.80;//Efficiency of the fluidized bed combustion system
+H=26;//The heating value of coal in MJ/kg
+S=3.6;//Sulphur content in the coal in %
+C=3;//The calcium sulphur ratio
+Ca=85;//The amount of calcium carbonate in the limestone in %
+CaCO3=100;//The molecular weight of CaCO3
+
+//Calculations
+Cb=O/(n*H);//Coal burning rate in kg/s
+Cb1=Cb*3600;//Coal burning rate in kg/h
+Sf=(Cb1*(S/100))/32;//Flow rate of sulphur in Kmol/h
+Cf=Sf*C;//The flow rate of calcium in Kmol/h
+Caf=Cf*CaCO3;//Mass flow rate of CaCO3 in kg/h
+L=Caf/(Ca/100);//Mass flow rate of limestone in kg/h
+
+//Output
+printf('The required flow rate of limestone is %3.1f kg/h ',L)
diff --git a/1943/CH5/EX5.5/Ex5_5.sce b/1943/CH5/EX5.5/Ex5_5.sce new file mode 100755 index 000000000..7cfceff4e --- /dev/null +++ b/1943/CH5/EX5.5/Ex5_5.sce @@ -0,0 +1,20 @@ + +clc
+clear
+//Input data
+CV=24;//The calorific value of the fuel in MJ/kg
+C=0.65;//The amount of calorific value released in the bed in %
+to=850;//Temperature at which products leave in degree centigrade
+ti=30;//The inlet temperature in degree centigrade
+tb=850;//The bed temperature in degree centigrade
+A=14.5;//The air fuel ratio by mass
+Cp=1.035;//The specific heat of the products leaving the bed surface in kJ/kgK
+B=7000;//The burning rate of coal in kg/h
+
+//Calculations
+H=(C*CV*1000)-(A*Cp*(to-ti));//Heat removal from the bed per kg fuel in kJ/kg fuel
+Hr=(H*B)/3600;//Rate of heat removal from the bed in kW
+Hb=(B/3600)*(1-C)*CV*1000;//The rate of heat removal from the above bed zone in kW
+
+//Output
+printf('(a) The rate of heat removal from the bed = %3.0f kW \n (b) The rate of heat removal from the above bed zone = %3.0f kW ',Hr,Hb)
diff --git a/1943/CH5/EX5.6/Ex5_6.sce b/1943/CH5/EX5.6/Ex5_6.sce new file mode 100755 index 000000000..12ab49288 --- /dev/null +++ b/1943/CH5/EX5.6/Ex5_6.sce @@ -0,0 +1,22 @@ + +clc
+clear
+//Input data
+tb=850;//The bed temperature in degree centigrade
+CV=25;//The calorific value of the fuel in MJ/kg
+A=9.5;//The stoichiometric air fuel ratio by mass
+E=20;//The amount of excess air used in %
+F=4.8;//The total fueling rate in MW
+p=0.3145;//The density of air at bed temperature in kg/m^3
+f=2;//The firing rate in MW/m^2
+v=2.7;//The fluidizing velocity in m/s
+
+//Calculations
+P=F/f;//Planform area in m^2
+m=(F*1000)/(CV*1000);//Fuel burning rate in kg/s
+ma=A*(1+(E/100))*m;//Mass flow rate of air in kg/s
+Pa=ma/(p*v);//Planform area in m^2
+
+//Output
+printf('(a) The planform area = %3.1f m^2 \n (b) Fuel burning rate = %3.3f kg/s \n Air flow rate = %3.4f kg/s \n Planform area = %3.2f m^2 ',P,m,ma,Pa)
+
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