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  • Users: joisy
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  1. joisy

    Foam Proportioners

    At our plant we used previously Fluorprotein Foam concentrate (CRODA) and we gonna change it over with AFFF. How do you think if it can cause a problem at the foam/water solution makers (the same concentration of foam concentrate & water - 3%) thanks, Joisy
  2. joisy

    Foam Proportioners

    At our plant we used previously Fluorprotein Foam concentrate (CRODA) and we gonnag change it over with AFFF. How do you think if it's a problem for the foam/water solution makers (the same concentration of foam concentrate & water - 3%) thanks, Joisy
  3. joisy

    Calculation Alarm/Trip Levels in 3-phase Flooded-Weir Separator

    Dear All, I've developed a software which calculates the alarm/trip levels (heights in meters) for the 3-phase Separators. They'r calculated on the base of the liquids' hold-up timings. (if the height of a particular level is less than some specific minimum value (meters), then it sets to this...
  4. joisy

    Low flow / high head requirements

    Dear All can you please advise me the vendor, which can supply the pump with 1 - 5 cub.m/h flow, 55 barg out and 2 m NPSHA. Assume that we should come up with positive displacement pump. thanks, Joisy
  5. joisy

    Petroleum Storage Tank Design

    Dear All, can you please advise me where (some practices ?) it's good to read about the cone bottoms' design (maybe with discharge well) for the Petroleum Storage Tanks. thanks, Joisy
  6. joisy

    Pump for oil/water sandy service

    Hello Everyone! I need to choose the pump for water/oil sandy service: the blend is to be pumped fro the atmospheric tank - 0.3 m static head to the vessel with 6 barg pressure. The blend contents the significant amount of sand - upto 3%. 80 cub.m/h is the required capacity can you please...
  7. joisy

    Pump for oil/water sandy service

    Hello Everyone! I need to choose the pump for water/oil sandy service: the blend is to be pumped fro the atmospheric tank - 0.3 m static head to the vessel with 6 barg pressure. The blend contents the significant amount of sand - upto 3%. 80 cub.m/h is the required capacity can you please...
  8. joisy

    Compressor Modelling via Hysys

    Hello All, can you please explain me the difference in modelling a compressor with & without characteristic curves thanks, Joisy
  9. joisy

    FAQ from Forum Tips

    Hello all, I do have some idea here ). Can someone (maybe from eng-tips) collect all the threads, sort them out by the topic and make them as a FAQ file - set for the downloading. This will help many people not to ask the same questions many times. Howevere this must be experienced engineer as...
  10. joisy

    Adiabatic Mode of Steam Flowing through the valve

    Hello All, can you please assist me with the particular problem. I do have the water steam (non-saturated) which enters the valve at 659 kPa(a) and 171 Deg C. At the outlet it has the pressure only 389 kPa(a). Assuming that proceeding process is adiabatic how to define the outlet temperature...
  11. joisy

    HYSYS Visual Basic

    Guys, maybe deviated from the subject of this forum... but has someone worked with the setting of user variables in HYSYS ? I do not have any info on how to work with HYSYS VB language and its objects. Can you advise me, please, where can I get such info? thanks, Joisy
  12. joisy

    HYSYS Visual Basic

    Guys, has someone worked with the setting of user variables in HYSYS ? I do not have any info on how to work with HYSYS VB language and its objects. Can you advise me, please, where can I get such info? thanks, Joisy
  13. joisy

    Fuel Gas Consumption /HYSYS

    Guys, is there any way to calculate how much fuel gas (MMSCFD) I need to have for example 1.4375e+07 Btu/hr of heat flow. The gas composition/temperature/pressure are known. I'd like to do it through the Hysys as the mix is very complex. Certainly I can comply the material balance and then to...
  14. joisy

    Intermediate results

    I'm currently with the solving of some very complex integral using the Mathcad. This opens in as the significantly simple expression. As I can see from the previous thread there is no way to see the intermediate steps?! Maybe there are the other programs (but MathCad), which allow it? cheers, Joisy
  15. joisy

    Diesel washing (flushing) with water to remove dissolved brine

    1) Has someone experienced with the flushing of the diesel with portable water and follow-up separation (via centrifuge) of the dissolved water to delute and remove the soluted sodium hydroxide? We use the bubbling method! 2) How it can be better achieved: to add dimulsifier to diesel and wash...
  16. joisy

    Diesel Flushing with Water

    1) Has someone experienced with the flushing of the diesel with portable water and follow-up separation (via centrifuge) of the dissolved water to delute and remove the soluted sodium hydroxide? We use the bubbling method! 2) How it can be better achieved: to add dimulsifier to diesel and wash...
  17. joisy

    Diesel water flushing

    1) Has someone experienced with the flushing of the diesel with portable water and follow-up separation (via centrifuge) of the dissolved water to delute and remove the soluted sodium hydroxide? We use the bubbling method! 2) How it can be better achieved: to add dimulsifier to diesel and wash...
  18. joisy

    Unit pressurization time

    Dear All, we do have the particular compressor system, connected to the gas/oil separator throgh the pipework. Before starting up the compressor unit (which consists of the three scrubbers, two coolers and two compressor' casings) should be pressurized by opening small 2" by-pass gas line...
  19. joisy

    New Scrubber Design

    All, my father has developed and even succesfully implemented the scrubber-absorber to clean the exhaust gases from SO2, H2S, and from dusts in the same time. He's got a local patent (in one of post USSR countries). Can you please advise me how this invention can be sold to the some...
  20. joisy

    Heat Exchager pressure losses

    Hello All, can you please advise the method/way to calculate dP across shell tube heat exchanger (operating with gas) thanks, Joisy

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