I would be happy to upgrade my associates degree into a degree in urban planning. Of course, this would have to be in the form of evening and weekend courses, as I would need to continue to work full time.
How can one quickly estimate the additional pressure drop to be introduced with more tube passes?
What is a good approximation for the heat transfer coefficient of hydrocarbons inside 3/4" tubes?
What is some good advice for specifying allowable pressure drops in shell and tube exchangers for heavy hydrocarbons?
Is it ever advantageous to use shells in series even though it may not be necessary?
What is the best way to control an oversized, horizontally oriented shell and tube steam heater?
Can condensate control in a reboiler cause water hammer problems?
What is a barometric condenser?
Why is a vacuum breaker used on shell and tube heat exchangers that are utilizing steam as the heating utility?
What could be a possible cause for sudden foaming in a cooling tower?
When specifying a cooling tower, should I look up historic wet bulb temperatures for my area or should I take measurements?
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