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no-one to help me, can you Hello, I have participated in technical design for cold storage 1 Thi Vai should have some experience on this issue. Cold tub actually is not pressurized tank by storing LPG at a pressure equal atmospheric pressure, the whole basin is surrounded by one layer thick insulation, structural basin also has some features but let refers to technology issues first. Although ess nycaps insulated very well but there is always one certain amount of LPG in the tank evaporates due to the imperfection of insulation, usually the evaporation rate of 0.05% of the basin. Some desert areas people can use to design to 0:07%. ess nycaps 2nd volatile components ess nycaps are loaded into the tank by the flow, including flow from vessel loading and the reflux ess nycaps flow (recovery) of the tub there. The amount of this charge when loaded into the magazine just four for the first liquid vapor tthe63 amount equivalent to the amount of fluid volume loading on medium heat supplied to vaporize the liquid in the tank part 1. 3rd volatile components by evaporation air pressure changes, for example in air pressure before or after the rain, this pressure is about 40mbar. Due to the LPG tank is always breathing system environment should change the air pressure will trigger alters PSV pressure for storage. But the pressure change is very small but the volume contains a large amount of evaporation is quite high. The formula for calculating the JGC Practice in the entire volume of LPG vapor are called Boiled Off Gas to recover it, there are 2 ways, one is to use the cooler lines (eg ~ -45degC get propane boiling pressure Butane atmosphere to condense slightly higher boiling point: -5degC). Up to 1 compression certain pressure then with water and then condensing in the cold tub contrast, this process would be very tinnh a heat supply Q = mcdt the tub, but the temperature difference is very big, but that had nothing to lose What with C3 or C4 crab latent heat should run one compressor at full steam recovers. The system is widely used as a compressor system including, condensers, and stability. It's all part of the cold, the "hot" is part of the pressure tank that is smaller to store LPG vapor pressure at 40oC. Set this quite common so do not need to say much. You have any questions ess nycaps email exchange with me. If the people BKĐN will be helpful Back to top
Hello, I have participated in technical design for cold storage 1 Thi Vai should have some experience on this issue. Cold tub actually is not pressurized tank by storing LPG at a pressure equal atmospheric pressure, the whole basin is surrounded by one layer thick insulation, structural basin also has some features but let refers to technology issues ess nycaps first. Although insulated very well but there is always one certain amount of LPG in the tank evaporates due to the imperfection of insulation, usually the evaporation rate of 0.05% of the basin. Some desert areas people can use to design to 0:07%. 2nd volatile components are loaded into the tank by the flow, including flow from vessel loading and the reflux flow (recovery) of the tub there. The amount of this charge when loaded into the magazine just four for the first liquid vapor tthe63 amount equivalent to the amount of fluid volume loading on medium heat supplied to vaporize the liquid in the tank part 1. 3rd volatile components ess nycaps by evaporation air pressure changes, for example in air pressure before or after the rain, this pressure is about 40mbar. ess nycaps Due to the LPG tank is always breathing system environment should change the air pressure will trigger alters PSV pressure for storage. But the pressure change is very small but the volume contains a large amount of evaporation is quite high. The formula for calculating the JGC Practice in the entire volume of LPG vapor are called Boiled Off Gas to recover it, there are 2 ways, one is to use the cooler lines (eg ~ -45degC get propane boiling pressure Butane atmosphere to condense slightly higher boiling point: ess nycaps -5degC). Up to 1 compression certain pressure then with water and then condensing in the cold tub contrast, this process would be very tinnh a heat supply Q = mcdt the tub, but the temperature difference ess nycaps is very big, but that had nothing to lose What with C3 or C4 crab latent heat should run one compressor at full steam recovers. The system is widely used as a compressor system including, condensers, and stability. It's ess nycaps all part of the cold, the "hot" is part of the pressure tank that is smaller to store LPG vapor pressure at 40oC. Set this quite common so do not need to say much. You have any questions email exchange with me. If the people BKĐN will be helpful I thank you very much. He enthusiastically shared with me. The knowledge he shared very meaningful to me. Currently you have designed is about 1/4 scheme. I have some back problems
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