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 --- 1073/CH6/EX6.16/6_16.sce | 41 +++++++++++++++++++++++++++++++++++++++++ 1 file changed, 41 insertions(+) create mode 100755 1073/CH6/EX6.16/6_16.sce (limited to '1073/CH6/EX6.16') diff --git a/1073/CH6/EX6.16/6_16.sce b/1073/CH6/EX6.16/6_16.sce new file mode 100755 index 000000000..98b1bcb50 --- /dev/null +++ b/1073/CH6/EX6.16/6_16.sce @@ -0,0 +1,41 @@ +clc; +clear; +//Example 6.16 +bpr=40.6; //[K] +Cpf=1.88; //[kJ/kg.K] +Hf=214; //[kJ/kg] +H1=505; //[kJ/kg] +mf_dot=4536; //[kg/h] of feed solution +ic=0.2; //Initial conc +fc=0.5; //Final concentration +m1dot_dash=(ic/fc)*mf_dot //Thisck liquor flow arte[kg/h] +mv_dot=mf_dot-m1dot_dash //[kg/H] +Ts=388.5; //Saturation temperature of steam in [K] +bp=362.5 //b.P of solution in [K] +lambda_s=2214; //[kJ/kg] +P=21.7; //Vapor space in [kPa] +Hv=2590.3; //[kJ/kg] + +//Enthalpy balance over evaporator +ms_dot=(m1dot_dash*H1+mv_dot*Hv-mf_dot*Hf)/lambda_s //[kg/h +printf("\nSteam consumption is %f kg/h\n",ms_dot); +dT=Ts-bp //[K] +U=1560 //[W/sq m.K] +Q=ms_dot*lambda_s //[kJ/h] +Q=Q*1000/3600 //[W] +A=Q/(U*dT) //[sq m] +printf("\nHeat transfer area is %f sq m\n",A); + +//Calculations considering enthalpy of superheated vapour + +Hv=Hv+Cpf*bpr //[kJ/kg] +ms_dot=(m1dot_dash*H1+mv_dot*Hv-mf_dot*Hf)/lambda_s //[kg/h] +printf("\n Now,Steam consumption is %f kg/h\n",ms_dot); +eco=mv_dot/ms_dot //Steam economy +printf("\nEconomy of evaporator %f\n",eco); +Q=ms_dot*lambda_s //[kJ/h] +Q=Q*1000/3600 //[w] +A2=Q/(U*dT) //Area +printf("\nNow,Area is %f\n",A); +perc=(A2-A)*100/A //%error in the heat transfer area +printf("\n If enthalpy of water vapour Hv were based on the saturated vapour at the pressure\nthe error introduced is only %f percent\n",perc); -- cgit