CHM ENG 150A Study Guide - Midterm Guide: Buckingham Π Theorem, Biproduct, Viscosity

17 views6 pages

Document Summary

You are tasked with designing a heat exchanger around a section of piping in a synthesis plant in which temperature control will be critical to prevent bi-product formation. In this process the temperature difference across the given length of pipe can be described as: T= t( , , v, c, q, d) where density, [kg/m^3], viscosity, [kg/(m*s)], velocity v[m/s], and heat capacity c. [j/(kg*k)] are fluid properties in the real system. D [m] is the diameter of the pipe, and q [j/s] is the total rate of heat input from the heat exchanger along entire surface area of the pipe considered. N3= (c t)/v2: you would like to run a model test on a cheaper fluid. The d and t are kept the same in the model system as the real setup. There is a selection of model fluids to choose from that all have cmodel =0. 25creal and model =0. 5 real.

Get access

Grade+20% off
$8 USD/m$10 USD/m
Billed $96 USD annually
Grade+
Homework Help
Study Guides
Textbook Solutions
Class Notes
Textbook Notes
Booster Class
40 Verified Answers

Related Documents

Related Questions