Recovery Method of Useful Components in Tail Gas in Acetic Acid Plant
A recovery method and a technology of a tail gas absorption tower, which are applied in separation methods, chemical instruments and methods, organic chemistry, etc., can solve the problems of large methanol consumption, large equipment investment, complex process, etc., and achieve energy saving, equipment investment and Operating costs, the effect of reducing volatilization
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Embodiment 1
[0025] use figure 1 The process shown. The tail gas absorption unit is provided with only one tail gas absorption tower, and the raw material methanol of the carbonylation reaction is used as the absorbent, and the tail gas from the reaction process and the tail gas from the rectification process directly enter the tail gas absorption tower. After treatment in the absorption tower, the top stream contains H 2 , CH 4 , N 2 , CO, CO 2 And a small amount of methanol can be directly sent to the flare system; the rich liquid at the bottom of the tower is mainly methanol, methyl iodide and a small amount of methyl acetate, which can directly lead to the reaction device.
[0026] In terms of weight percentage, the tail gas from the reaction process includes: methane 4.2%, CO 40.5%, CO 2 14.7%, iodomethane 25.5%, pressure is 0.3MPa. The tail gas from the distillation process includes: methane 6.4%, CO 35.2%, CO 2 7.2%, 28.7% of methyl iodide, and a pressure of 0.21MPa. The total feed co...
Embodiment 2
[0038] use figure 1 The process shown. In terms of weight percentage, the tail gas from the reaction process includes: 8% methane, 31% CO, CO 2 8.0%, iodomethane 35%, pressure is 0.3MPa. The tail gas from the distillation process includes: methane 6.2%, CO 45%, CO 2 8.0%, 21% methyl iodide, pressure 0.21MPa. The total feed composition of the tail gas absorption tower is: hydrogen 0.1%, methane 7.3%, nitrogen 5.7%, CO36.2%, CO211.7%, methanol 873ppm, methyl iodide 29.8%, methyl acetate 9.0%, and acetic acid 0.1%. The temperature of the absorbent methanol is 10°C. The pressure of the absorption tower is 0.2MPa.
[0039] The results of the absorption treatment are shown in Table 3. The recovery rate of methyl iodide reaches 100%, and the heat load of the methanol cooler is 247.3KW.
[0040] table 3
[0041] Component Top flow of absorption tower (wt%) Bottom flow of absorption tower (wt%) H20.000609041.4925e-07 CH 4 0.119413820.00017200 N20.095852624.1167e-05 CO0.592856420.000...
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