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 --- 2873/CH12/EX12.2/Ex12_2.jpg | Bin 0 -> 491339 bytes 2873/CH12/EX12.2/Ex12_2.sce | 55 ++++++++++++++++++++++++++++++++++++++++++++ 2 files changed, 55 insertions(+) create mode 100755 2873/CH12/EX12.2/Ex12_2.jpg create mode 100755 2873/CH12/EX12.2/Ex12_2.sce (limited to '2873/CH12/EX12.2') diff --git a/2873/CH12/EX12.2/Ex12_2.jpg b/2873/CH12/EX12.2/Ex12_2.jpg new file mode 100755 index 000000000..d184d992b Binary files /dev/null and b/2873/CH12/EX12.2/Ex12_2.jpg differ diff --git a/2873/CH12/EX12.2/Ex12_2.sce b/2873/CH12/EX12.2/Ex12_2.sce new file mode 100755 index 000000000..9be21c9ae --- /dev/null +++ b/2873/CH12/EX12.2/Ex12_2.sce @@ -0,0 +1,55 @@ +// Display mode +mode(0); +// Display warning for floating point exception +ieee(1); +clear; +clc; +disp("Engineering Thermodynamics by Onkar Singh Chapter 12 Example 2") +h1=40;//average heat transfer coefficient at inner surface in KJ/m^2 hr oc +h6=50;//average heat transfer coefficient at outer surface in KJ/m^2 hr oc +deltax_steel=2*10^-3;//mild steel sheets thickness in m +deltax_wool=5*10^-2;//thickness of glass wool insulation in m +k_wool=0.16;//thermal conductivity of wool in KJ/m hr +k_steel=160;//thermal conductivity of steel in KJ/m hr +T1=25;//kitchen temperature in degree celcius +T6=5;//refrigerator temperature in degree celcius +disp("here thermal resistances are") +disp("R1=thermal resistance due to convection between kitchen air and outer surface of refrigerator wall(T1 & T2)") +disp("R2=thermal resistance due to conduction across mild steel wall between 2 & 3(T2 & T3)") +disp("R3=thermal resistance due to conduction across glass wool between 3 & 4(T3 & T4)") +disp("R4=thermal resistance due to conduction across mild steel wall between 4 & 5(T4 & T5)") +disp("R5=thermal resistance due to convection between inside refrigerator wall and inside of refrigerator between 5 & 6(T5 & T6)") +disp("overall heat transfer coefficient for one dimentional steady state heat transfer") +disp("(1/U)=(1/h1)+(deltax_steel/k_steel)+(deltax_wool/k_wool)+(deltax_steel/k_steel)+(1/h6)") +disp("so U=1/((1/h1)+(deltax_steel/k_steel)+(deltax_wool/k_wool)+(deltax_steel/k_steel)+(1/h6))in KJ/m^2hr oc") +U=1/((1/h1)+(deltax_steel/k_steel)+(deltax_wool/k_wool)+(deltax_steel/k_steel)+(1/h6)) +U=2.8;//approx. +disp("rate of heat transfer(Q)=U*A*(T1-T6)in KJ/m^2 hr") +disp("wall surface area(A) in m^2") +A=4*(1*0.5) +Q=U*A*(T1-T6) +disp("so rate of heat transfer=112 KJ/m^2 hr ") +disp("Q=A*h1*(T1-T2)=k_steel*A*(T2-T3)/deltax_steel=k_wool*A*(T3-T4)/deltax_wool") +disp("Q=k_steel*A*(T4-T5)/deltax_steel=A*h6*(T5-T6)") +disp("substituting,T2=T1-(Q/(A*h1))in degree celcius") +T2=T1-(Q/(A*h1)) +disp("so temperature of outer wall,T2=23.6 oc") +disp("T3=T2-(Q*deltax_steel/(k_steel*A))in degree ") +T3=T2-(Q*deltax_steel/(k_steel*A)) +disp("so temperature at interface of outer steel wall and wool,T3=23.59 oc") +disp("T4=T3-(Q*deltax_wool/(k_wool*A))in degree celcius") +T4=T3-(Q*deltax_wool/(k_wool*A)) +disp("so temperature at interface of wool and inside steel wall,T4=6.09 oc") +disp("T5=T4-(Q*deltax_steel/(k_steel*A))in degree celcius") +T5=T4-(Q*deltax_steel/(k_steel*A)) +disp("so temperature at inside of inner steel wall,T5=6.08 oc") + + + + + + + + + + -- cgit