⟩ Suppose if I use Window->Close without saving my model, have I lost my work?
No, still the model can be retrieved from session until you use command Erase not displayed.
No, still the model can be retrieved from session until you use command Erase not displayed.
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?
What kind of concerns is associated with temperature pinch points in condensers?
When an expansion is joint needed on the shell side of a shell and tube heat exchanger?
When should one be concerned with the tube wall temperature on the cooling waterside of a shell and tube exchanger?
Can large temperature differences in vaporizers cause operational problems?
What effect does choking a vertical thermosiphon have on the heat transfer rate?
What is a good relation to use for calculating tube bundle diameters?
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?