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I am so sorry gr2vessels. I should have been more clear. This is not for a heat exchanger it's just a natural gas "knock-out drum". The media is water and hydrocarbon vapors, with a density of 0.064 lb/ft^3. The flow is listed on the data sheet as 95,938 lb/hr and 46.11 MMSCFD. Operating...

Hello all, I have been asked to design an impingement plate per the horizontal vessel detail on page 390 of the Pressure Vessel Design Manual (top right of page) by Dennis R. Moss. Procedure 5-13 shows a vertical vessel but not a horizontal vessel and in all honesty I'm at a loss as to the...

Sorry for the late reply, I've been out of town lately. Thank you fairlane46, and all the others. If anyone else has anything for me to research please add it to my list. You all are a valuable resource for me and I appreciate the help immensely.

Excellent! Thank you everyone for the responses and valuable information. Some more info: 1.)I appreciate everyone's concern about liability because that is exactly why I am asking. 2.)I would never just buy a program and start using it. There is functionality in my current software platform...

Hello all and I thank you for your time in advance. I am new to the forum and even newer to pressure vessel design. One of my clients fabricates ASME pressure vessels. One of the tasks my company performs is creating the shop fabrication drawings for these vessels for them. We have been doing...