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Recent content by franklin55

  1. franklin55

    ASME U-Stamp for Surface condenser designed on FV

    Is the ASME designed condenser heavier than the HEI design? I am asking this because the vendors has told us that if we want to build it as per ASME the weight will increase by 15 ~ 20%. Consequently it will affect the cost.
  2. franklin55

    ASME U-Stamp for Surface condenser designed on FV

    Actually we require ASME U-stamp for ensuring the quality and safety. Is there any other means in case the condenser is designed to HEI which we can use as a safeguard? (just like U-Stamp in case of ASME)
  3. franklin55

    ASME U-Stamp for Surface condenser designed on FV

    We are procuring a surface condenser.The heat transfer area of the condenser is around 3500 m2.and one of our requirement mentioned in the RFQ is that the condenser should be U-Stamped. Some of the vendors have replied that since condensers are designed for negative pressure (Full Vacuum),and...
  4. franklin55

    How to open a stuck butterfly valve

    "DLiteE30 (Mechanical) 24 Aug 11 16:31 Wow, that's hard to believe. The stem broke when trying to open it with wrench, but you were able to push it open with a rod. Huh. " The yoke from large sized valve was removed and installed on pipe near the valve (with stem going inside pipe through...
  5. franklin55

    How to open a stuck butterfly valve

    "macmet (Materials) says 24 Aug 11 9:24 Is this valve in service all year round? " The answer is "Yes"
  6. franklin55

    How to open a stuck butterfly valve

    We have partially succeeded in opening of the valve by inserting a rod into pipe through a hole made in the pipe and pushing valve gate through it. To achieve full flow, bypass was installed by hot tapping. However there is a problem if we need to close the valve in future. How to close the...
  7. franklin55

    How to open a stuck butterfly valve

    Its schedule 20 pipe. The cooling water pressure is 5 Kg/cm2.the temperature of the water is around 35 degree centigrade
  8. franklin55

    Opening of in-service Butterfly valve with broken locking pin

    we have installed two bypass lines across this valve by ho tapping ( 10" and 12 "), but still the required flow is not passing through it. (Because the cross sectional area of 12" and 10" is less than the area of 24").
  9. franklin55

    How to open a stuck butterfly valve

    We have a 24" Wafer type butterfly valve installed on the inlet cooling water line of one of the exchangers.A few days back the valve was closed for taking the exchanger out of service for maintenance purpose. After the maintenance we tried to take the exchange back into service by opening the...
  10. franklin55

    Opening of in-service Butterfly valve with broken locking pin

    We have a 24" Wafer type butterfly valve installed on the inlet cooling water line of one of the exchangers.A few days back the valve was closed for taking the exchanger out of service for maintenance purpose. After the maintenance we tried to take the exchange back into service by opening the...
  11. franklin55

    NDE Sequence of newly installed piping

    Thank you for replying.But is there any reference mentioning the same.
  12. franklin55

    NDE Sequence of newly installed piping

    We have installed new piping for natural gas service. The QA/QC have advised its 100% RT followed by hydrostatic test. But we want to have the hydrostatic test first because the situation is such that we can save some time if we do the hydrostatic test first. Does code place some restriction on...
  13. franklin55

    Leakage from welded diaphragm gasket of Heat Exchanger

    Thanks rmw for advice. Your assumption is right, the heater cannot be isolated from the rest of the plant. It needs shutdown of the whole plant (Ammonia Plant. The exchanger is Synthesis converter effluent converter and cools raw synthesis gas with cooling water. We will do this job with our...
  14. franklin55

    Leakage from welded diaphragm gasket of Heat Exchanger

    We have tried to tighten the bolts in the vicinity of the leak point, and the leakage actually increased. We have a spare diaphragm but for replacing the diaphragm we have to shutdown the plant (2-3 days outage) which we are trying to avoid. Now in case if the leakage further increases and we...

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