I have existing boiler (4MMBtu/hr), and the condensate return from the Process side is going directly to Boiler Feed Water Tank. Plant is not in use since last couple of years and client is planning t

I got a exchanger which is operated on a temperature control, the condendate load is about 2600 lb/hr The operating pressure is 60 psig and the condensate is drained to atmosphere.

At present time, my company intent to distribute/utilized the steam which generate from Co-Gen Plant to several facilities.. The Steam pipelines app.length is 20 km. Need your advise regarding the pip

I have noticed there is a spec break after the steam trap (at outlet flange of a manual valve just downstream the steam trap) and that the ratings upstream and downstream the steam trap are significan

Trying to correct another writer on a political/science type discussion page, but am at a job site and don't have my usual "fundemental" engineering reference books.