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  • Users: PSP113
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  1. PSP113

    Stack Opacity Affected By Rain

    Hello. I work in a coal-burning power plant. We have noticed that during a couple heavy downpours recently, our stack opacity has gone up significantly for short periods and then returned to normal. The opacity meter is situated about half way up our stack. Can anyone offer suggestions why...
  2. PSP113

    Anhydrous Ammonia Venting

    We are installing an anhydrous ammonia tank in our coal burning power plant to inject for flue gas conditioning. My question has to do with the loading by truck of the product. The tank will be at 600 kPag (14°C) to 815 kPag (22°C), so when we fill the tank, the truck driver will equalize the...
  3. PSP113

    CSA Z662 Hydro test pressure

    Hello, Does anyone know what the hydrotest pressure for CSA Z662 is supposed to be. I know it's 1.5 times design for B31.3, but I can't recall what Z662 is.
  4. PSP113

    Asphaltenes in TEG system

    We have two mechanical refrig. plants that dehydrate sales gas by spraying TEG into the gas-gas exchangers. We are having an issue where asphaltenes drop out of the gas and become entrained in the TEG. When it cycles back, the nozzles get plugged and if we can't clear the plug with a pressure...
  5. PSP113

    BTEX vapour mitigation

    We have a satellite with a TEG dehy system. The water that gets removed from the regenerated TEG goes to a holding tank that is currently open to atmosphere. This water contains BTEX and the vapour has a strong odour. I know two options of getting rid of this nuisance are a vapor recovery...
  6. PSP113

    B16.5 Flange Ratings

    Does anyone know the difference between A182 F316 and A182 F316L Flanges? They have the same amount of Cr, Ni, and Mo, but have different pressure ratings and they are categorized in different material groups.
  7. PSP113

    Ethylene Glycol for Heating

    We use ethylene glycol for our heat tracing. The boiler that we use for heating the glycol was re-tubed two years ago, and it just started leaking 3 months ago. Upon inspection, we found several tubes corroded around the area on the tube attached to the tube sheet(they're attached by rolling)...
  8. PSP113

    [b]Fuel Gas as a Blanket[/b]

    We are thinking of using fuel gas as a blanket for our ethylene glycol storage tank. The boiler for the glycol is downstream approx. 10-15 feet away. Is it a bad idea to have a fuel gas blanket on a vessel so close to an ignition source. Does anyone know what code or standard gives spacing...
  9. PSP113

    CO2 and hydrates

    We have multiple wells in a relatively mature oil field. In the last year we set up a pilot project to inject C02 into the formation to get greater oil production. Within the last six months we've seen hydrate formation across the choke spools on our wells. This causes interuption in...
  10. PSP113

    Liquid CO2 piping design

    What material of piping is best for liquid CO2 at 230-250 psig? Does B31.3 have a table of suitable materials for specific fluids?
  11. PSP113

    Bushing issues

    My pipefitter has issues with using bushings. I've heard of others not liking the practice of using bushings, but no one can explain why. The only thing I've been able to find is that the lack of "meat" in a bushing doesn't lend much confidence to it's pressure rating. My feeling is if a...
  12. PSP113

    ASME Section VIII and re-rating a vessel's MAWP

    I was looking through Section VIII on how to re-rate a vessel's MAWP. At first crack, it seems all I can do is use the design calculations and hope the manufacturer underrated the vessel. Does anyone have any experience with this?

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