What should be the heat distribution in the middle section of the atmospheric and vacuum distillation column in a light crude oil atmospheric and vacuum distillation unit?
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I would like to ask what the heat distribution at the middle section of the atmospheric and vacuum distillation columns in a light crude oil atmospheric and vacuum distillation unit should be What should the temperature difference for mid-section reflux be?
A large flow rate and low temperature difference facilitate the removal of heat from high-temperature areas. After heat removal, the side-stream distillation temperature should be such that it meets the product quality requirements
If it is a running device, try to extract as much heat from the high-temperature side as possible. If it is during the design phase, it is best to optimize the heat extraction distribution and the temperature level for heat extraction by taking into account the pinch points of the heat exchange network.
Heat extraction should be based on the quality of your product! The return flow rate will be different if the device is different; it depends on the actual conditions for determining the return flow rate
The value obtained using the grip software is 264 degrees; how can heat distribution be optimized in light of this?
Try to avoid having the heat extraction temperature changes cross the pinch point area; generally, about 80% of heat extraction occurs in the middle section of atmospheric pressure columns, while 90% occurs in vacuum columns. Under conditions that ensure product quality, as much heat as possible should be extracted from higher positions
The heat extraction ratio between No. 1 and No. 2 plants is 60:50, with a temperature difference of 70~110℃
Please send me your email address: mpcchuang@163.com. I will send you a guide on the optimal temperature, temperature difference, and operational optimizations for atmospheric pressure mid-stage reflux, based on my experience
My email address is june_zi@126.com
My email address is june_zi@126.com
364760441@qq.com