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A shell-and-tube Heat exchanger with one shell exceed and two tube passes si to be designed to condense 3900 kg/hr of steam at 1 atm. Steam may be suppose to enter the shell side as a saturated vapor and leave as a saturated liquid. Water is used as cooling fluid in tubes with an inlet temperature of 40 oC. Consider over heat transfer coefficient values from Table:10.1, Verify a suitable design which specifies
(a)Number of tubes in every pass,
(b) outlet water temperature,
(c) tube diameter and length in every tube pass, and
(d) mass flow rate of water and final inside diameter of the shell that may needed.
The over all diffinition of stripping
when do the cell get alot of thing in there thing because am confuse cause is alot of thing becaus is crazy
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objective of the nasic test
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1. Consider the previous heat exchanger. Tune a proportional controller for a) GM = 2; PM = 45 degrees and c) MPH (maximum peak height) occurs at 2 dB (provides a z of ~ 0.4).
counter current extraction
a mixture of propane (125 lbmole, K = 2.056), n-butane (200 lbmole, K = 0.925), and n-pentane (175 lbmole, K=0.520), is at 200 psia and 200 F. determine the phase of the mixture?
Which one of the following statements is correct? You may wish to examine a molecular model of this compound. 1. Carbon G is an asymmetric center and its configuration is R 2
absorbtion
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