Method for purifying crude isophthalic acid oxidation slurry
A technology for crude isophthalic acid and oxidation slurry, which is applied in the field of purification of crude isophthalic acid oxidation slurry, and can solve the problems of increasing the acetic acid-water solution process and its energy consumption
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Embodiment 1
[0034] Such as figure 1 and 2 As shown, take 2000 grams of oxidation reactor 1 and obtain the crude isophthalic acid oxidation slurry-flash slurry I6 obtained by three-stage decompression flash evaporation, wherein the temperature of the first stage decompression flash evaporation is 201 ° C, and the flash The steaming pressure is 11.62kg / cm 2 , the temperature of the second-stage decompression flash is 159°C, and the pressure of the flash is 4.59kg / cm 2 , the temperature of the third-stage decompression flash is 92°C, and the pressure of the flash is 0.50kg / cm 2 , the flash slurry I6 enters into a pressure difference of 2.5kg / cm through the slurry pump 5 under the following physical property conditions 2 The first stage 23 of the rotary drum filter press 10 of the rotary drum filter press performs pressure filtration: the space velocity is 22hr -1 , by weight percentage, isophthalic acid 26.79%, catalyst 0.21%, acetic acid concentration 64.50%, other impurities 8.50%, tem...
Embodiment 2~3
[0036] Such as image 3 , 4 As shown in 5 and 6, only the first oxygen-containing flow-air purge times and the second oxygen-containing flow-air purge stages in Example 1 are changed. The results are shown in Table 1.
Embodiment 4
[0038] Only the purging step of the oxygen-containing stream in Example 1 was removed, and the others were correspondingly kept unchanged. The results are shown in Table 1. It can be seen from the data in Table 1 that if the oxygen-containing flow purging step is omitted, the filter cake VIII12 will still have a large amount of m-xylene in addition to the high residual amount of acetic acid, requiring other complicated post-treatment procedures.
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