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Hi guys, We had a situation of extremely hot tubes in the primary reformer. Our process is desulphurised natural gas and steam. Here's the problem... After shutdown of the unit for mechanical repairs, the delta P on the reformer increased by 15 psi and the dropped by 5 psi. Subsequent surveys...

Hi, this is the problem.............we need to reduce catalyst......a copper catalyst. in a reactor.......our carrier gas for the procedure is methane. In the past a great deal of gas was flared off after passing thru the reactor, we seek to recover it for environmental and economic reasons...

Hi, I would like to know the specific reasonoing for not warming up the condensing steam tubine withsteam thru the T&T valve.