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  1. Jasmine2000

    pressure vessel

    Why is unusual? Is that beacuse no one has done it yet?
  2. Jasmine2000

    pressure vessel

    I am trying to design a pressurized vessle for gasoline storage tank. This vessel will have relief valve. How can I calculate the pressure rise in the vessel with temperature rise? This vessel will have nitrogen blanketing? Gasoline is volatile I do nor think I can use ideal gas law. Please...
  3. Jasmine2000

    vapor recovry

    I have already contacted these two companies. It requires PSA system which is very expensive for such a small plant.
  4. Jasmine2000

    vapor recovry

    I am working on vapor recovery system and there are mixture of gasoline and ethaol. The following describes the system design: The vapor recovery system will have nitrogen blanketing at each tank, the vapor recovery system will utilize a vent condenser to condense vapor ethanol and traces of...
  5. Jasmine2000

    blanketing tank with CO2

    IS THERE ANY REASON THAT A TANK CAN NOT BE BLANKETED WITH CO2 INSTEAD OF NATURAL GAS OR N2? THANKS
  6. Jasmine2000

    FALMMABILITY CALCULATION

    How can I calculate flammibility of gasoline vapor by knowing vapor pressure, UEL and LEL, and total pressure?
  7. Jasmine2000

    nitrogen blanketing

    I am working on vapor recovery system. I am trying to collect gasoline and ethaol vapors. the client does not want to blanket the tanks. tanks are open to atmosphere. any idea? I am trying to find a source such as API to document it. I have NFPA 30 but it doesn't cover blanketing requirements...
  8. Jasmine2000

    gasoline

    There is a gasoline tank and I am trying to calculate the LEL % AND UEL% BASED ON VAPOR PRESSURE. ANY IDEA HOW TO DO THIS? THE TEMPERATURE IS 100F AND PRESSURE IS 14.7 PSIA
  9. Jasmine2000

    safety reilef valve

    There is an SRV at the discharge of a heat exchanger the MAWP of this equipment is 270 psig and srv set pressure is set @ 270 psig. pump is pumping at 244 psig down stream of the HX. During the start up and shut down of the unit the srv leaked. The client I am working with he believes the srv...
  10. Jasmine2000

    connversion of caustic tank to H2SO4 storage.

    Dear ash9144 Most of the sufuric acid storage tanks have N2 blanketing why there is no need for 98% H2SO4?
  11. Jasmine2000

    connversion of caustic tank to H2SO4 storage.

    I am working on converting an existing caustic tank to 98% sulfuric acid. The tank is made of A-36 and is atmospheric. I believe moisture ingression into the tank would dilute the concentration, consequently increasing the corrosion rate.for this reason, I am planning to blanket the tank with...

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