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author | priyanka | 2015-06-24 15:03:17 +0530 |
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committer | priyanka | 2015-06-24 15:03:17 +0530 |
commit | b1f5c3f8d6671b4331cef1dcebdf63b7a43a3a2b (patch) | |
tree | ab291cffc65280e58ac82470ba63fbcca7805165 /2510/CH11 | |
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 '2510/CH11')
-rwxr-xr-x | 2510/CH11/EX11.10/Ex11_10.sce | 12 | ||||
-rwxr-xr-x | 2510/CH11/EX11.11/Ex11_11.sce | 12 | ||||
-rwxr-xr-x | 2510/CH11/EX11.12/Ex11_12.sce | 35 | ||||
-rwxr-xr-x | 2510/CH11/EX11.13/Ex11_13.sce | 12 | ||||
-rwxr-xr-x | 2510/CH11/EX11.14/Ex11_14.sce | 25 | ||||
-rwxr-xr-x | 2510/CH11/EX11.15/Ex11_15.sce | 10 | ||||
-rwxr-xr-x | 2510/CH11/EX11.16/Ex11_16.sce | 15 | ||||
-rwxr-xr-x | 2510/CH11/EX11.17/Ex11_17.sce | 24 | ||||
-rwxr-xr-x | 2510/CH11/EX11.3/Ex11_3.sce | 9 | ||||
-rwxr-xr-x | 2510/CH11/EX11.4/Ex11_4.sce | 14 | ||||
-rwxr-xr-x | 2510/CH11/EX11.5/Ex11_5.sce | 11 | ||||
-rwxr-xr-x | 2510/CH11/EX11.6/Ex11_6.sce | 10 | ||||
-rwxr-xr-x | 2510/CH11/EX11.7/Ex11_7.sce | 13 | ||||
-rwxr-xr-x | 2510/CH11/EX11.8/Ex11_8.sce | 10 | ||||
-rwxr-xr-x | 2510/CH11/EX11.9/Ex11_9.sce | 18 |
15 files changed, 230 insertions, 0 deletions
diff --git a/2510/CH11/EX11.10/Ex11_10.sce b/2510/CH11/EX11.10/Ex11_10.sce new file mode 100755 index 000000000..234813c06 --- /dev/null +++ b/2510/CH11/EX11.10/Ex11_10.sce @@ -0,0 +1,12 @@ +//Variable declaration: +TH = 140.0+460.0 //Absolute outside temperature of pipe (ft^2) +TC = 60.0+460.0 //Absolute temperature of surrounding atmosphere (ft^2) +A = 10.0 //Area of pipe (ft^2) +E = 0.9 //Emissivity of pipe + +//Calculation: +Q = E*A*0.173*((TH/100.0)**4-(TC/100.0)**4) //Heat loss due to radiation (Btu/h) +Q = round(Q*10**-1)/10**-1 + +//Result: +printf("The heat loss due to radiation is : %f Btu/h.",Q) diff --git a/2510/CH11/EX11.11/Ex11_11.sce b/2510/CH11/EX11.11/Ex11_11.sce new file mode 100755 index 000000000..ded3aa878 --- /dev/null +++ b/2510/CH11/EX11.11/Ex11_11.sce @@ -0,0 +1,12 @@ +//Variable declaration: +//Froma example 11.10: +Q = 880.0 //Heat loss due to radiation (Btu/h) +A = 10.0 //Area of pipe (ft^2) +TH = 140.0 //Absolute outside temperature of pipe (°F) +TC = 60.0 //Absolute temperature of surrounding atmosphere (°F) + +//Calculation: +hr = Q/(A*(TH-TC)) //Radiation heat transfer coefficient (Btu/h.ft^2.°F) + +//Result: +printf("The radiation heat transfer coefficient is : %.1f Btu/h.ft^2.°F.",hr) diff --git a/2510/CH11/EX11.12/Ex11_12.sce b/2510/CH11/EX11.12/Ex11_12.sce new file mode 100755 index 000000000..d808e5af5 --- /dev/null +++ b/2510/CH11/EX11.12/Ex11_12.sce @@ -0,0 +1,35 @@ +//Variable declaration: +D = 0.0833 //Diameter of tube (ft) +L = 2.0 //Length of tube (ft) +h = 2.8 //Heat transfer coefficient (Btu/h.ft^2.°F) +Ta1 = 1500.0+460.0 //Temperature of hot air in furnace (°R) +Ta2 = 1350.0+460.0 //Temperature of hot air in the furnace brick walls (°R) +Tt = 600.0+460.0 //Surface temperature of tube (°R) +E = 0.6 //Surface emissivity of tube +s = 0.1713*10**-8 //Stefan-Boltzmann constant +pi = %pi + +//Calculation: +//Case 1: +A = pi*D*L //Area of tube (ft^2) +Qc = round(h*A*(Ta1-Tt)*10**-1)/10**-1 //Convection heat transfer from air to tube (Btu/h) +Qr = round(E*s*A*(Ta2**4-Tt**4)*10**-2)/10**-2 //Radiation feat transfer from wall to tube (Btu/h) +Q = Qr+Qc //Total heat transfer (Btu/h) +//Case 2: +Qp = Qr/Q*100 //Radiation percent +//Case 3: +hr = Qr/(A*(Ta2-Tt)) //Radiation heat transfer coefficient (Btu/h.ft^2.°F) +//Case 4: +T = Ta2-Tt //Temperature difference (°F) + +//Result: +printf("1. The convective heat transferred to the metal tube is : %f Btu/h.",Qc) +printf(" The radiative heat transferred to the metal tube is : %f Btu/h.",Qr) +printf(" The total heat transferred to the metal tube is : %f Btu/h .",Q) +printf("2. The percent of total heat transferred by radiation is : %.1f %%.",Qp) +printf("3. The radiation heat transfer coefficient is : %.1f Btu/h.ft^2.°F.",hr) +if (T > 200) then + printf("4. The use of the approximation Equation (11.30), hr = 4EsTav^3, is not appropriate.") +elseif (T < 200) then + printf("4. The use of the approximation Equation (11.30), hr = 4EsTav^3, is appropriate.") +end diff --git a/2510/CH11/EX11.13/Ex11_13.sce b/2510/CH11/EX11.13/Ex11_13.sce new file mode 100755 index 000000000..813920638 --- /dev/null +++ b/2510/CH11/EX11.13/Ex11_13.sce @@ -0,0 +1,12 @@ +//Variable declaration: +Q = 5.0 //Radiation heat transfer (W) +E = 1.0 //Emissivity of filament +s = 5.669*10**-8 //Stefan-Boltzmann constant +T1 = 900.0+273.0 //Light bulb temperature (K) +T2 = 150.0+273.0 //Glass bulb temperature (K) + +//Calculation: +A = Q/(E*s*(T1**4-T2**4)) //Surface area of the filament (m^2) + +//Result: +printf("The surface area of the filament is : %.2f cm^2",A*10**4) diff --git a/2510/CH11/EX11.14/Ex11_14.sce b/2510/CH11/EX11.14/Ex11_14.sce new file mode 100755 index 000000000..91ab7fd9a --- /dev/null +++ b/2510/CH11/EX11.14/Ex11_14.sce @@ -0,0 +1,25 @@ +//Variable declaration: +T1 = 127.0+273.0 //Surface temperature (K) +T2 = 20.0+273.0 //Wall temperature (K) +T3 = 22.0+273.0 //Air temperature (K) +s = 5.669*10**-8 //Stefan-Boltzmann constant +e = 0.76 //Surface emissivity of anodized aluminium +D = 0.06 //Diameter of %pipe (m) +L = 100.0 //Length of %pipe (m) +h = 15.0 //%pipe convective heat transfer coefficient (W/m^2.K) + +//Calculation: +Eb = s*T1**4 //Emissive energy of %pipe (W/m^2) +E = e*Eb //Emissive power from surface of %pipe (W/m^2) +A = %pi*D*L //Surface area of %pipe (m^2) +Qc = h*A*(T1-T3) //Convection heat transfer to air (W) +Qr = e*s*A*(T1**4-T2**4) //Radiation heat transfer rate (W) +Q = Qc+Qr //Total heat transfer rate (Btu/h) +Tav = (T1+T2)/2.0 //Average temperature (K) +hr = 4*e*s*Tav**3 //Radiation heat transfer coefficient (W/m^2.K) + +//Result: +printf("The emissive power from surface of %%pipe is : %.0f W/m^2.",E) +printf("The convection heat transfer to air is : %.1f kW.",Qc/10**3) +printf("The radiation heat transfer rate is : %.1f kW",Qr/10**3) +printf("The radiation heat transfer coefficient is : %.1f W/m^2.K.",hr) diff --git a/2510/CH11/EX11.15/Ex11_15.sce b/2510/CH11/EX11.15/Ex11_15.sce new file mode 100755 index 000000000..6d61ab3f2 --- /dev/null +++ b/2510/CH11/EX11.15/Ex11_15.sce @@ -0,0 +1,10 @@ +//Variable declaration: +//From example 11.14: +Qc = 15.0 //Convection heat transfer coefficient (W/m^2.K) +hr = 7.2 //Radiation heat transfer coefficient (W/m^2.K) + +//Calculation: +X = hr/(Qc+hr)*100.0 //Percent heat transfer by radiation (%) + +//Result: +printf("The percent heat transfer by radiation is : %.1f %%.",X) diff --git a/2510/CH11/EX11.16/Ex11_16.sce b/2510/CH11/EX11.16/Ex11_16.sce new file mode 100755 index 000000000..9b7dbbfec --- /dev/null +++ b/2510/CH11/EX11.16/Ex11_16.sce @@ -0,0 +1,15 @@ +//Variable declaration: +FV = 1.0 //Correction factor +//From example 11.9: +FE = 0.358 //Emissivity correction factor +TH = 300.0+460.0 //Absolute temperature of external surface (°R) +TC = 75.0+460.0 //Absolute temperature of duct (°R) +AH = 0.622 //Area of pipe (ft^2) +s = 0.173*10**-8 //Stefan-Boltzmann constant + +//Calculation: +Q = FV*FE*AH*s*(TH**4-TC**4) //Heat transfer rate (Btu/h.ft) + +//Result: +printf("The heat transfer rate is : %.2f Btu/h.ft",Q) +printf("Since, Q obtained in (11.9) is 96.96 Btu/h.ft, the solution does not match with book.") diff --git a/2510/CH11/EX11.17/Ex11_17.sce b/2510/CH11/EX11.17/Ex11_17.sce new file mode 100755 index 000000000..46e7f8b55 --- /dev/null +++ b/2510/CH11/EX11.17/Ex11_17.sce @@ -0,0 +1,24 @@ +//Variable declaration: +//From figure 11.2: +L = 1.0 //Space between plates (m) +X = 0.5 //Length of plate (m) +Y = 2.0 //Width of plate (m) +s = 5.669*10**-8 //Stefan-Boltzmann constant +TH = 2000.0+273.0 //Temperature of hotter plate (K) +TC = 1000.0+273.0 //Temperature of colder plate (K) +Btu = 0.2934*10**-3 //Btu/h in a KW + +//Calculation: +A = X*Y //Area of plate (m^2) +Z1 = Y/L //Ratio of width with space +Z2 = X/L //Ratio of length with space +//From figure 11.2: +FV = 0.18 //Correction factor +FE = 1.0 //Emissivity correction factor +Q1 = FV*FE*s*A*(TH**4-TC**4) //Net radiant heat exchange between plates (kW) +Q2 = Q1/Btu //Net radiant heat exchange between plates in Btu/h (Btu/h) +Q1 = round(Q1*10**-2)/10**-2 + +//Result: +printf("The net radiant heat exchange between plates is : %f kW.",Q1) +printf("The net radiant heat exchange between plates in Btu/h is : %.2f x 10^8 Btu/h.",Q2/10**8) diff --git a/2510/CH11/EX11.3/Ex11_3.sce b/2510/CH11/EX11.3/Ex11_3.sce new file mode 100755 index 000000000..0af8b179b --- /dev/null +++ b/2510/CH11/EX11.3/Ex11_3.sce @@ -0,0 +1,9 @@ +//Variable declaration: +syms l //Wavelength (mu.m) +I = 40*exp(-l**2) //Intensity of radiation (Btu/h.ft^2.mu.m) + +//Calculation: +E = eval(integrate(I, l,0,%inf)) //Total emissive power (Btu/h.ft^2) + +//Result: +printf("The total emissive power is : %.1f Btu/h.ft^2.",E) diff --git a/2510/CH11/EX11.4/Ex11_4.sce b/2510/CH11/EX11.4/Ex11_4.sce new file mode 100755 index 000000000..a31d594c6 --- /dev/null +++ b/2510/CH11/EX11.4/Ex11_4.sce @@ -0,0 +1,14 @@ +//Variable declaration: +l = 0.25 //Wavelength (mu.m) +//From equation 11.4: +lT = 2884 //Product of wavelength and absolute temperature (mu.m.°R) + +//Calculation: +T = lT/l //Sun's temperature (°R) +T1 = round(T * 10**-2)/10**-2 +T = T - 460 +T460 = round(T * 10**-3)/10**-3 + +//Result: +printf("The Sun s temperature is : %f °R.",T1) +printf("The Sun s temperature in fahrenheit scale is : %f °F.",T460) diff --git a/2510/CH11/EX11.5/Ex11_5.sce b/2510/CH11/EX11.5/Ex11_5.sce new file mode 100755 index 000000000..d2c3cfd5b --- /dev/null +++ b/2510/CH11/EX11.5/Ex11_5.sce @@ -0,0 +1,11 @@ +//Variable declaration: +T1 = 1500.0+460.0 //Absolute temperature 1 (°R) +T2 = 1000.0+460.0 //Absolute temperature 2 (°R) + +//Calculation: +X = T1**4/T2**4 //Ratio of quantity of heat transferred +x = 100*(T1**4-T2**4)/T2**4 //Percentage increase in heat transfer (%) + +//Result: +printf("The ratio of the quantity/rate of heat transferred is : %.2f .",X) +printf("The percentage increase in heat transfer is : %.0f %%",x) diff --git a/2510/CH11/EX11.6/Ex11_6.sce b/2510/CH11/EX11.6/Ex11_6.sce new file mode 100755 index 000000000..46239f3ac --- /dev/null +++ b/2510/CH11/EX11.6/Ex11_6.sce @@ -0,0 +1,10 @@ +//Variable declaration: +T1 = 1200.0+460.0 //Absolute temperature of wall 1 (°R) +T2 = 800.0+460.0 //Absolute temperature of wall 2 (°R) + +//Calculation: +//From equation 11.23: +X = 0.173*((T1/100.0)**4-(T2/100.0)**4) //Heat removed from colder wall (Btu/h.ft^2) + +//Result: +printf("The heat removed from the colder wall to maintain a steady-state is : %.0f Btu/h.ft^2.",X) diff --git a/2510/CH11/EX11.7/Ex11_7.sce b/2510/CH11/EX11.7/Ex11_7.sce new file mode 100755 index 000000000..afaca937d --- /dev/null +++ b/2510/CH11/EX11.7/Ex11_7.sce @@ -0,0 +1,13 @@ +//Variable declaration: +s = 0.173 //Stefan-Boltzmann constant (Btu/h.ft^2.°R) +EH = 0.5 //Energy transferred from hotter body (Btu/h.ft^2) +EC = 0.75 //Energy transferred to colder body (Btu/h.ft^2) +TH = 1660.0 //Absolute temperature of hotter body (°R) +TC = 1260.0 //Absolute temperature of colder body (°R) + +//Calculation: +E = s*((TH/100.0)**4-(TC/100.0)**4)/((1.0/EH)+(1.0/EC)-1.0) //Net energy exchange per unit area (Btu/h.ft^2) +E = round(E*10**-1)/10**-1 + +//Result: +printf("The net energy exchange per unit area is : %f Btu/h.ft^2.",E) diff --git a/2510/CH11/EX11.8/Ex11_8.sce b/2510/CH11/EX11.8/Ex11_8.sce new file mode 100755 index 000000000..936f56aaf --- /dev/null +++ b/2510/CH11/EX11.8/Ex11_8.sce @@ -0,0 +1,10 @@ +//Variable declaration: +//From example 11.6-11.7: +E1 = 8776.0 //Energy exchange between black bodies (Btu/h.ft^2) +E2 = 3760.0 //Energy exchange between non-black bodies (Btu/h.ft^2) + +//Calculation: +D = (E1-E2)/E1*100 //Percent difference in energy (%) + +//Result: +printf("The percent difference relative to the black body is: %.1f %%.",D) diff --git a/2510/CH11/EX11.9/Ex11_9.sce b/2510/CH11/EX11.9/Ex11_9.sce new file mode 100755 index 000000000..504fb2449 --- /dev/null +++ b/2510/CH11/EX11.9/Ex11_9.sce @@ -0,0 +1,18 @@ +//Variable declaration: +s = 0.173*10**-8 //Stefan-Boltzmann constant (Btu/h.ft^2.°R) +TH = 300.0+460.0 //Absolute temperature of external surface (°R) +TC = 75.0+460.0 //Absolute temperature of duct (°R) +//From Table 6.2: +AH = 0.622 //External surface area of pipe (ft^2) +//From Table 11.2: +EH = 0.44 //Emissivity of oxidized steel +AC = 4.0*1.0*1.0 //External surface area of duct (ft^2) +EC = 0.23 //Emissivity of galvanized zinc + +//Calculation: +FE = 1.0/(1.0/EH+((AH/AC)*(1.0/EC-1.0))) //Emissivity correction factor +Q = FE*AH*s*(TH**4-TC**4) //Net radiation heat transfer (Btu/h.ft) + +//Result: +printf("The net radiation heat transfer is : %.2f Btu/h.ft^2.",Q) +printf("There is a calculation error in book.") |