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  1. boonchoo2211

    Pressure Vessel and Pressure Equipmt

    Hello all, What is the different between the Pressure Vessel and Pressure Equipment ? I understand that the different is just only the design pressure which the pressure will be greater than 15 PSI as per ASME VIII Div 1 code. I have the Desender Hydrocyclone package which the design pressure...
  2. boonchoo2211

    How to prevent the liquid enter to the Hg Removal Unit

    Hello All, The natural gas from the 1st Separator (Three phase) go to the Filter coalescer and then go to the Hg removal unit. Now we face the problem that high amount of free liquid and aerosol detected on the Hg removal unit. It is difficult for the absorbent loading out that we have to dig...
  3. boonchoo2211

    Remove the suction scrubber from the compressor train

    I just wonder that why do we need the scrubber though we have the 1st stage separator installed upstream. I know that the 1st will never work with 100% effeciency but I will install the heater or the coalescer instead. Is this a good idea in order to save cost? Prutiew
  4. boonchoo2211

    Remove the suction scrubber from the compressor train

    Hello all, I am a mechanical engineer who change the working field to the process engineer. This is my first time for posting my question here.I have the suction scrubber installed between the 1st stage separator and compressor for natural gas system. Is it possible to remove the suction...
  5. boonchoo2211

    Split Case vetically mounted Vs Vertical In-line

    In my opinion the advantages of the vertical inline pump over Split case vertically mounted pumps are 1) Direct installation in the pipeline,so minimal space required 2) No alignment of pump and driver 3) No baseplate, coupling or guard Disadvantages:limited to weight of the motor drive Prutiew
  6. boonchoo2211

    impeller

    The power dissipation of a mixing impeller is given by the following correlation: P = N*p*N3D5/1000 where: P = power dissipation, kW N = power number, dimensionless p = fluid density at conditions, kg/m3 N = impeller rotational speed, revis D = impeller diameter, m Prutiew

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