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  • Users: NghiaPP
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  1. NghiaPP

    Crew compressor as make-up compressor

    In hydrotreating process, the make-up hydrogen is supplied by a make-up compressor with discharge pressure in the range 50 to 90 bar. Suction pressure is around 20 bar. Gas purity is 90% H2 or higher. All make-up compressors, I have seen are of reciprocating type with a stand-by machine. The...
  2. NghiaPP

    Help to vessel specification

    I need some guidelines to make specification for a distillation column. The vessel shall be designed according to ASME VIII div. 2. Design pressure is 8 bar and design temperature is 250 deg.C, , material is CS. As a consequence of a up set condition, the vessel could be filled up with liquid...
  3. NghiaPP

    Mechanical coupling control valves

    Hi all, I design a temperature controller for a heat exchanger. A by-pass line around one side is used to control the outlet temperature. The size of the main line and bypass line is large (14"), such as a three-way valve is not desired. A layout with two butterfly valves is suggested. But...
  4. NghiaPP

    Replace DEA with MDEA to increase capacity

    I'm working in a project to find a way to increase the capacity of an amine absorber. The amine absorber is installed in a diesel HDS unit to remove H2S from the recycle gas. In the future, sulphur in the feed will increase by 50% and the H2S amount to be removed is expected 50% higher. The...
  5. NghiaPP

    Maximal temperature for high head pump

    I 'm interesting to know what is the maximal temperature a high head pump can work ? The pumping fluid is gas oil at few bars on suction side. Discharge pressure is 50 to 100 bar. The question is raised when I want to recover as much as possible heat from the low pressure section of the plant...

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