Method for purifying crude isophthalic acid oxidized sizing agent
A crude isophthalic acid and slurry technology, applied in the separation/purification of carboxylic acid compounds, organic chemistry, etc., 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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