Rectifying section tower bottom reboiling internal heat-integrated energy-saving rectifying apparatus and method
A rectification section and rectification technology, applied in the field of rectification, can solve the problems affecting the normal operation and service life of the compressor, the negative impact on process safety and smooth operation, and the heat load is not recovered and utilized, etc., to achieve wide industrial application Prospects, improvement of feed heat conditions, and effect of reducing operating costs
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Embodiment 1
[0035] Embodiment one (typical ideal system separation)
[0036] Situation 1: The method of the present invention is used for the separation of benzene-toluene system, and the process described in the present invention is adopted. The feed position is the top of the stripping section, the feed amount is 1000kg / h, the feed composition is 50% (wt%), and the feed temperature is 20°C. The number of theoretical plates in the rectification section and the stripping section is 34, and the feeding position is the top of the stripping section. The operating pressure of the stripping section is normal pressure, and the operating pressure of the rectifying section is 2.5atm. The output of the overhead product in the rectification section is 500kg / h, the purity of the extracted product is controlled above 99% (wt%), and the superheated temperature of the gas superheater at the top of the stripping section is 10°C. In this case, the heat provided by condensation at the top of the rectifi...
Embodiment 2
[0105] Embodiment two (typical non-ideal system separation)
[0106] Situation 1: Separation of ethanol-water system, using the process described in the present invention. The feed position is the top of the stripping section, the feed amount is 1000kg / h, the feed composition is 50% (wt%), and the feed temperature is 20°C. The number of theoretical plates in the rectification section and the stripping section is 36, and the feeding position is the top of the stripping section. The operating pressure of the stripping section is normal pressure, and the operating pressure of the rectifying section is 2.5atm. The output of the overhead product in the rectification section is 500kg / h, the purity of ethanol in the extracted product is controlled above 92% (wt%), and the superheated temperature of the gas superheater at the top of the stripping section is 10°C. In this case, the heat provided by condensation at the top of the rectification section is greater than the sum of the he...
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