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: PKEngineer
  • Content: Threads
  • Order by date
  1. PKEngineer

    Pipeline Valve Change Out

    We are in a situation of replacing multiple 16” 600# gate valves with ball valves installed on natural gas pipeline. Both type of valves has same face to face dimensions. Problem we are facing is that this pipeline is in a seismic fault zone and we have feeling that pipeline is under stress and...
  2. PKEngineer

    Looking for equipment alternatives to separate waxy solids from Pipeline Gas

    My company is looking for alternatives to free pipeline (12 inch) gas from entrained solids upstream of valve station. Few years back this line was being used for transferring crude oil before switching it to gas. Line has been pigged more than one time after switching but instruments (including...
  3. PKEngineer

    Load Monitors Reliability For Mag Drive Pumps

    On our LPG/LNG facility we use sealless pumps for LPG, caustic soda and ammonia services ranging from 1-40 HP. LPG mag drive pumps (40 HP) were originally supplied with power monitors for pump protection against no/low/ high flows plus some other inherent mag pumps troubles. Our I&E department...
  4. PKEngineer

    Missing U-1A Forms/ NB#

    As working on equipment filing structure for a recently owned company I found few things which I am not sure: 1: Equipment files for old ones like manufactured before late 1960s have no ASME U-1A forms. On the other hand , new equipments have there U-1A Forms and also national board number on...
  5. PKEngineer

    Pipeline Leak Detection Threshold Values

    As per regulatory compliance and safety concerns we need to set alarm setpoints for the maximum flow rate and response time if any leak detection occurs. I read somewhere: In State of Washington, it is mandatory for all pipeline operators to be able to detect and locate leaks of 8 percent of...
  6. PKEngineer

    Pump making more Differential Head than rated

    Could anyone explain possible reason(s) for having more differential head through centrifugal pump than rated (more than shut-in pressure)for liquid butane service pumping from suction sphere. Flow rate is within the operating range as measured? I would assume suction and discharge pressure...
  7. PKEngineer

    Maximum velocity and pressure drop limits for pumps piping

    Could I get guidance to find out the capacity of light hydrocarbon lines (butane) both for centrifugal pump suction and discharge piping? What is the industry standard for maximum velocity and pressure drop limits. I know API RP 14E recommends 3 ft/sec and 9 ft/sec max for velocities for suction...

Part and Inventory Search