Probs5,11,17

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The document provides details on two problems involving heat exchanger design and optimization. Problem 11 involves designing a condenser to condense 2000 kg/hr of vapor at 132°C using cooling water. The optimal solutions are a cooling water flow rate of 2284.58 kg/hr and an exit temperature of 106.54°C. Problem 17 requires determining the optimal exit temperature and optimal tube length but no other details are provided.

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[object Object],Where hf is in W/m 2 -k, T w and T s in O C and L in m

Given: ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],REQUIRED: x opt

Problem No. 11 ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]

Problem No. 11 ,[object Object],[object Object],[object Object],[object Object],[object Object],[object Object]

Problem No. 11 ,[object Object],[object Object],[object Object],[object Object],[object Object]

Problem No. 11 ,[object Object],[object Object],[object Object],[object Object]

Given Required: a.) t2opt b.) L opt of tubes

People often look surprised when I tell them that Thermodynamics was probably one of my favorite classes in school. This was the final project for my Thermo II class and was intended to be done in groups. I wanted to challenge myself to a near unnecessary limit by completing this entire project myself. The purpose of this project was to determine the optimum operating pressure for the feedwater heater for a power cycle (from a selected problem in the textbook). However the primary focus, and most difficult task, was writing a program in C++ to calculate multiple values for a selected problem in our textbook. I quite literally had to teach myself how to program in C++ well beyond the basics I had learned in an intro class. This program had to be capable of cross referencing multiple reference tables in the back of the book, each having dozens of values which had to be manually typed in. Which reference tables it pulled values from was dependent on the user inputted turbine efficiency and feedwater heater pressure. It easily took me over a month to debug and test this program to ensure it was always going to the correct reference tables to pull data when outputting the calculations it performed. Update on 7/2/2016: I did attempt to make another program that would allow the user to type in any feedwater heater pressure rather than make a selection from values there was a reference table for in the back of the back. The program used a method of interpolation to obtain all the data needed to perform all the calculations that were outputted. I don't remember the last time I attempted to run that version of the program, but I seem to recall getting impossible answers outputted. This indicated to me that a more complicated method of interpolating values was required, or I just couldn't get it to work correctly. I ultimately decided against pursuing that version of the program any further. Just getting it work correctly with a predefined list of pressures to select from was difficult enough.

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Probs5,11,17

1. Plant Design and Economics Problem Set De Vera, Armel John Opena, Kristine Joy Usman, Leonides Vistan, Rhovee

6. computed T w ≠ assumed T w !

7. computed T w ≠ assumed T w !

9. computed T w = assumed T w ! cm

10.

11.

12.

13.

14.

15.

16. Solution to Problem 17 Group V 5ChE-B

17. Given Required: a.) t2opt b.) L opt of tubes

18. Solution

19. Solution

Probs5,11,17

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