Basic Programs for Chemical Engineers by Dennis Wright (auth.)

By Dennis Wright (auth.)

The microcomputer has positioned an unlimited quantity of computational strength within the arms of the training chemical engineer. besides the fact that, a microcomputer is of little use until there are courses on hand to resolve chemical engineer­ ing difficulties; during this ebook, i've got prepare a set of simple professional­ grams that w~ll support the working towards engineer be extra effective and ready to clear up advanced difficulties which are as a rule dealt with on mainframe com­ puters. The plant engineer will locate the booklet really worthwhile. The plant en­ gineer is calle~ upon to enquire difficulties that diversity from easy hassle taking pictures to tQe precise layout of complicated chemical vegetation. the bigger proj­ ects are typically add-on jobs to the normal tasks of holding a chemical plant operating. In t~day's enterprise weather, solutions to difficulties has to be received quick and ~ccurately. the pc is able to checking out speculation, thereby allo~ing engineers to judge replacement options to difficulties quick and supply solutions to management's questions that constantly shift just like the sand~ in a desert.

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OF PASSES? 10,2 TUBE FLUID: FOULING FACTOR =0 NAME OF FLUID, FOULING FACTOR? 0005 TEMP IN(F}=0 TEMP OUT(F) = 0 SPECIFIC HEAT (BTUlLB-F)=0 TEMP IN, TEMP OUT, SPECIFIC HEAT? 85,100,1 VISCOSITY(CP) = 0 DENSITY (LB/FT3) =0 VISCOSITY, DENSITY? (BTUIFT-HR-F}=0 THERMAL COND.? 345 MASS FLOW (LB/HR)=0 MASS FLOW? 100000 SHELL PASSES = 0 SHELL ID (INCHES) =0 NO. OF SHELL PASSES, SHELL ID? 1,12 NO. OF BAFFLES =0 BAFFLE SPACING (INCHES) =0 NO. OF BAFFLES, BAFFLE SPACING? 30,4 HEAT TRANSFER 37 SHELL FLUID: FOULING FACTOR=O NAME OF FLUID, FOULING FACTOR?

820/0. Compound B is virutally consumed after 2 hr. 5%. , pp. 72-73. 5R(3,C) Nomenclature for DIFFEQ VARIABLE Xl(C)n Xl(C)n + 1 F(C) DT R(N,C) DESCRIPTION Integrated value at T Integrated value at T + DT Differential equation Step size Runge-Kutta derivations EXAMPLE READY RUN SIMULTANEOUS LINEAR DIFF EQUATIONS NO. OF EQUATIONS =? 4 TIME INTERVAL, STEP SIZE=? 10 INITIAL VALUE OF X(1)=? 10 INITIAL VALUE OF X(2) =? 10 INITIAL VALUE OF X(3) =? 0 INITIAL VALUE OF X(4) =? 0 PRINT INTERVAL =? 10 ****PROGRAM RUNNING**** CALCULATIONS COMPLETED .....

00 PITCH = TRIANGULAR SQUARE(S} OR TRIANGULAR(T} PITCH? T TUBE LENGTH (FT) =0 NUMBER OF PASSES =0 TUBE LENGTH, NO. OF PASSES? 10,2 TUBE FLUID: FOULING FACTOR =0 NAME OF FLUID, FOULING FACTOR? 0005 TEMP IN(F}=0 TEMP OUT(F) = 0 SPECIFIC HEAT (BTUlLB-F)=0 TEMP IN, TEMP OUT, SPECIFIC HEAT? 85,100,1 VISCOSITY(CP) = 0 DENSITY (LB/FT3) =0 VISCOSITY, DENSITY? (BTUIFT-HR-F}=0 THERMAL COND.? 345 MASS FLOW (LB/HR)=0 MASS FLOW? 100000 SHELL PASSES = 0 SHELL ID (INCHES) =0 NO. OF SHELL PASSES, SHELL ID? 1,12 NO.

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