Continue to Site

Eng-Tips is the largest engineering community on the Internet

Intelligent Work Forums for Engineering Professionals

  • Congratulations waross 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: *

  • Users: rusman
  • Content: Threads
  • Order by date
  1. rusman

    What is typical Plant Availability for Crude Oil Storage Tank Terminal

    Hello my virtual friends and expertise! We are currently performing feasibility study for the crude oil storage tank terminal and pipeline. In the terminal there will be few storage tanks (more than 30) and a series of pumping station. The required no of pump is series is 13 nos (assuming all...
  2. rusman

    Any experience and knowledge on Hydraulic Lift?

    Hi there... Does anybody know and have any experience on the Hydraulic Lift system for enhance recovery of the well? I know one of the method for enhance recovery is using Gas Lift, ESP, Gas Injection and water injection. Any source of info abt Hydraulic Lift system is highly appreciated. Thanks!
  3. rusman

    Standard available motor size in the market

    I need to know the standard available motor size in the market, used for the refinery and petrochemical industry. If possible I need to know the power factor and the efficiency (at full load) of such motor. Any help is highly appreciated. Thanks!!!
  4. rusman

    Pipeline design pressure for ASME B31.8 pipe

    Hi there. I Have a problem.. If one wanna design the topside piping design based on B31.3, we have to look the pressure and temperature rating based on ASME B16.5 to check the MAWP for the specific design temperature for the specific material. But, if I want to design gas pipeline, which using...
  5. rusman

    Process Licensor for Triple Phosphate Plant.

    Hello folks. I'm working with Design Consultant company, currently seeking the Process Licensor for making Triple Phosphate Plant. Anybody know the know-how of the process. Thanks Rusman Process Engineer
  6. rusman

    Safe limit of SS316L under H2S sour environment

    Anybody knows the safe limit of SS316L for H2S sour environment system? My problem is, H2S pp is 2.2 psia, Cl ion is 10,000 ppm(wt) max, ph +- 6.5, free water present when process upset.

Part and Inventory Search