Currently I am responsible for mentoring my own junior CAD drafter. My current company puts a large emphasis on mentorship and it was a huge compliment to me when I was asked to be a mentor to someone newer to their career. This is because I have a higher than average level of knowledge in regards to our systems, and projects.
Is there a handy way to determine if a horizontal pipe is running full if the flow rate is known?
How is plate heat exchangers used in an ammonia refrigeration system?
Is there a difference in MTD (Mean Temperature Difference) between "E" and "J" (Divided Flow) type shell and tube heat exchangers?
Are there any alternatives to scraping a shell and tube if a capacity increase will make the pressure drop across the exchanger too large?
Are some heat transfer services more prone to tube vibration that others for a shell and tube exchanger?
What is a good method of minimizing shell side pressure drop in a shell and tube exchanger?
What are some of the consequences of an undersized kettle type reboiler?
What are some good strategies for curing tube vibration in shell and tube exchangers?
What factors go into designing the vapor space of kettle type reboiler?
Is there a quick rule-of-thumb to estimate a gas side heat-transfer rate inside the tubes of a shell and tube heat exchanger?
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