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  • Users: chengg29
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  1. chengg29

    Obtaining stream results at the end of every operating condition for a ASPEN PLUS simulation

    Hi, Currently I am running a steady state simulation, on ASPEN PLUS (I have only a few years of experience in the usage of ASPEN PLUS), for a Pharmaceutical plant. It's a batch process and I am using a BATCHSEP model in this simulation. The feed comprises Na2co3 along with Dichloromethane...
  2. chengg29

    Corrosion issues in an existing RFCC unit of a refinery

    Hi, As part of an ongoing exercise in the company to debottleneck a 70 KBPD existing refinery one of the issues that needed a resolution was the corrosion issues in an RFCC unit in order to debottleneck it. Following below are options to debottleneck the same, which under discussion right now...
  3. chengg29

    FSE Certification for a Process Engineer

    Hello folks, I am not sure whether this post belongs here but considering the fact that the other forums do not seem to discuss what I wish to state in my post I thought that this may be the most appropriate foreum of them all :) I am a Process Design / Systems Engineer with 20 plus years of...
  4. chengg29

    Modelling of HPRT in HYSYS

    Hi, I am trying to model a Hydraulic Power Recovery Turbine (HPRT) in a Steady State simulation on HYSYS. As far as I can think I have two options to do it: a) Use a PUMP module. When the simulation converges the Pump icon is outlined with a yellow line around the pump icon with a warning...
  5. chengg29

    MDEA Absorber using Hydroxy Ethyl Piperazine (HEP) as promoter- HYSYS simulation problems

    Hi all, I have recently simulated an AGRU design on HYSYS Ver. 8.8 using Acid Gas package as a thermodynamic package and using the Acid Gas template provided as part of HYSYS Ver 8.8 simulator package. This AGRU plant design utilizes HEP, instead of Piperazine, as a promoter to MDEA solvent in...

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