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  1. GarethChem

    Commissioning standards

    Hi EmmanuelTop and sshep It's quite suprising to me that API doesn't have commissioning standards, they even have standards on hydrotesting tanks (API 650). Thanks for the help! Gareth
  2. GarethChem

    Commissioning standards

    Hi everyone I just wanted to find out if anyone knows if there is an API standard or similar for commissioning (particularly for a tank farm). Thanks! Gareth
  3. GarethChem

    Low Pressure Vessel Pressure Protection

    I agree 100% with everyone else. You definitely require a PSV and should do a HAZOP. Even though you will never operate at 1375psi, you need to remember if there is a fire, the metal weakens and pressure increases. PSVs are very reliable (0.01 - 0.67 faults/year for a 1/1 system...
  4. GarethChem

    PRV resetting frequency

    Hi everyone I have tried searching for an answer on the forums and google and can't find anything conclusive. I used to work for a company who said that every time that a PRV lifted, it had to be taken out and reset as the spring became unreliable (though this was never done in practice, this...
  5. GarethChem

    Thermal relief on LPG lines

    Thanks for the article Snorgy. BigInch - Why's that? A 15m (50ft) length of 200NB pipe (8") is just less than 0.5m3. To me, if a line that size is liquid full, it'd be a serious problem, especially if it is one of the lines just after the outlet nozzle of the LPG sphere... Or am I missing...
  6. GarethChem

    Thermal relief on LPG lines

    I agree, an excessive amount of TRVs is the only thing I can think of. Thanks everyone, glad to see I'm not the only one that thought that it was necessary for small volumes too :) BigInch - you said it'd work for you, do you mean that you agree with the FEED (i.e. not required on smaller...
  7. GarethChem

    Fire protection

    Hi Shunoff There are a lot of NFPAs, the ones that I've used on tank farms so far are: NFPA 11 - Standard for Low Expansion Foam NFPA 13 - Installation of Sprinkler systems NFPA 16 - Standard for the Installation of Foam-Water Sprinkler and Foam-Water Spray Systems NFPA RP 14G - Recommended...
  8. GarethChem

    Thermal relief on LPG lines

    Hi everyone I read the following in a FEED: "LPG - any section more than 500L of LPG that can be blocked in shall be provided with a TRV." Do you have any idea why there is a limit to the smallest volume that requires a TRV? I'd imagine a rupture in the line or flange or a failing gasket is...
  9. GarethChem

    Hot work safe distance from live plant

    It's gasoil & mogas... I am not sure if it was designed properly, though I know everything is EX except motors are IP56. Thanks for the help though! Will definitely have to see if they are even using work permits o.O Hopefully they are. But I know it's so remote that they don't have water to...
  10. GarethChem

    Hot work safe distance from live plant

    Thanks LittleInch. I figured it would probably have something to do with the electrical zone ratings, was hoping for a "20m from pumps" kind of an answer :) They didn't do zone classification for this plant - working in Africa is veeeery different....
  11. GarethChem

    Newb qc question

    Hi Welderturnedqc, and welcome If I can add to what the other guys said - the flange rating also has to do with the operating temperature - the higher the operating temperature, the lower the pressure rating. You might find this link useful, it has the pressure ratings for a few different...
  12. GarethChem

    Jet A-1 contamination

    I never said thanks for your feedback BigInch and LittleInch, so thanks :)
  13. GarethChem

    Hot work safe distance from live plant

    Hi all I have been asked to commission a tank and am concerned about future work on site. They will be continuing with hot work a little distance from the tank while the tank has been commissioned (though it will be a different system). I haven't been to this particular site yet so the distance...
  14. GarethChem

    Jet A-1 contamination

    Thanks so much BigInch - I thought there might be a bit of contamination allowed (since Jet A1 and Diesel have overlapping carbon chain lengths, I figured that only C16-C21 would be contaminants). Seems it is a lot more complicated than that! Thanks for the info! You seems to always have the...
  15. GarethChem

    Jet A-1 contamination

    Hi again! I am researching the possibility of multi-product pipelines, and need to know how much diesel (gasoil) or gasoline (mogas) is alllowed to contaminate Jet A-1. From what I've read, it seems the limiting factor may in fact be the water in the diesel and gasoline, rather than the...
  16. GarethChem

    Vapour pressure question

    25362 - Makes sense, I thought that when pressurised, the propane would condense pretty quickly (though I have no grounds to think this happens quickly - I guess this is just something I imagined and never questioned it) LittleInch - thanks :) Since there's no weigh bridge, we only measure the...
  17. GarethChem

    Vapour pressure question

    Hi LittleInch Thanks for your patience. I think I understand what you're saying - basically the gas is in transient state and in a sort of aerosol? How did you calc the 15bara, IGL? I think the answer from the drivers tomorrow will clear things up. I wish the guys had installed a vapour...
  18. GarethChem

    Vapour pressure question

    Would the lighter-than-LPG hydrocarbons be able to exert that much pressure? The way I see it, the vapour pressure exerted by a single component in a mixture is approx. the mol fraction * Pvap (Raoult's law) and even if there were lighter components, the molar frac should be small enough that it...
  19. GarethChem

    Vapour pressure question

    I can't - I was wondering about that today as well, maybe it hasn't reached equilibrium. We have 4 tankers coming back tomorrow and I should recognise a couple of the drivers so I'll ask them :)

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