Continue to Site

Eng-Tips is the largest engineering community on the Internet

Intelligent Work Forums for Engineering Professionals

  • Congratulations KootK on being selected by the Eng-Tips community for having the most helpful posts in the forums last week. Way to Go!

Search results for query: *

  1. mthausif123

    Selecting vessel head for design pressure > 90 barg

    Thank you all for your responses. My senior has asked me to explore the possibility of using a full flange flat head instead of an ellipsoidal or hemispherical head. The reason given is that there is just one nozzle on the head, and its size is less than half the size of the vessel. Given this...
  2. mthausif123

    Selecting vessel head for design pressure > 90 barg

    Hi. I am designing a pressure vessel whose design pressure is >90 barg. There are some internals inside the vessels hence inspection is required. I cannot install a manhole because the shell ID < 1000 mm. Can I provide flanged head? And what type of head? Ellipsoidal or spherical?
  3. mthausif123

    4 tube passes in TEMA D front head

    Hi, is it allowable to opt for 4 tube passes (U-tube) in an exchanger with TEMA D type front head (High pressure gas). The vapor fraction inlet/outlet tube side is: 100/92 percentage respectively.
  4. mthausif123

    Tube material for DM water

    Could you kindly explain the advantages of using SS316L even when the water is already clean?
  5. mthausif123

    TEMA G shell for liquids

    Hi, I want to confirm whether TEMA G shell can be used for liquids flowing in shell side.
  6. mthausif123

    Tube material for DM water

    Hi, I want to know whether carbon steel tubes are suitable for an heat exchanger to handle demineralized water flowing in shell side in closed loop, i.e., the demineralized water does not contact with air. Assuming tube side fluid is non-corrosive.
  7. mthausif123

    For any heat exchanger design (pres

    Thank you, Christine and Littleinch, for helping me out.
  8. mthausif123

    For any heat exchanger design (pres

    CS stands for Carbon steel. Sorry for not mentioning clearly.
  9. mthausif123

    For any heat exchanger design (pres

    For any heat exchanger design (pressure < 50 barg) I consider tube thickness of 2.11 mm for CS and 1.65 mm for SS. As per my understanding 2.11 - 1.65 = 0.46 mm is extra thickness for CS as corrosion allowance. Is my understanding correct?
  10. mthausif123

    Steam/carbon ratio calculation.

    George, I also received an answer to this query from another source. Steam inlet to SMR is also used for the shift reaction (CO + H2O ---> CO2 + H2). So CO concentration should be included but not CO2.
  11. mthausif123

    Steam/carbon ratio calculation.

    For calculating the steam/carbon ratio at the inlet of a steam methane reformer, should CO and CO2 concentrations be included?
  12. mthausif123

    Is CS a suitable material for cooling water with high chloride content?

    Hi, Thank you everyone. I understand that CS is not suitable for my case. I am opting for SS316L instead.
  13. mthausif123

    Is CS a suitable material for cooling water with high chloride content?

    Hi, I am designing a cooler with open recirculating tower cooling water as cooling media. Tube side fluid is cooling water. The maximum chloride content of cooling water is 500 wt ppm. I have selected carbon steel as tube material. Client has raised concerns whether I can guarantee 10 years...

Part and Inventory Search