Treatment process of water-insoluble VOCs waste gas
A water-insoluble, treatment process technology, applied in the field of water-insoluble VOCs waste gas treatment process, can solve the problems of low VOCs purification efficiency, VOCs tail gas not up to standard, large amount of absorbent, etc., to reduce the amount, realize recycling, The effect of reducing operating costs
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Embodiment 1
[0037] use as figure 1 The shown water-insoluble VOCs waste gas treatment process has a concentration of 12000mg / m for a pharmaceutical company 3 The exhaust gas of butyl acetate (the air volume is 800m 3 / h) for processing, the specific process is as follows:
[0038] In this example, the water-insoluble VOCs specifically refers to butyl acetate.
[0039] The exhaust gas treatment process containing butyl acetate in this embodiment includes two exhaust gas absorption units arranged in series, that is, the first-end absorption tower 2 and the second-stage absorption tower 3 . The absorbent enters the secondary absorption tower 3, and the exhaust gas containing butyl acetate enters from the first-end absorption tower 2, and cross-flow contacts with the absorbent in the first-end absorption tower 2, and the absorbent in the first-end absorption tower 2 is mixed with acetic acid The volume ratio of the waste gas of butyl ester is 1:60, so that butyl acetate is enriched in the ...
Embodiment 2
[0046] use as figure 2 The shown water-insoluble VOCs waste gas treatment process has a concentration of 81000mg / m for a chemical company 3 Xylene waste gas (air volume is 1200m 3 / h) for processing, the specific process is as follows:
[0047] In this embodiment, the water-insoluble VOCs specifically refer to xylene.
[0048] The exhaust gas treatment process containing xylene in this embodiment includes three exhaust gas absorption units arranged in series, namely the head-end absorption tower 2 , the second-stage absorption tower 3 and the third-stage absorption tower 4 . The absorbent enters the third-stage absorption tower 4, and the exhaust gas containing xylene enters from the head-end absorption tower 2, and cross-flow contacts with the absorbent in the head-end absorption tower 2, so that the xylene is enriched in the absorbent. In the embodiment, the absorbent is specifically N-ethylpyrrolidone, and the volume ratio of the absorbent in the head-end absorption tow...
Embodiment 3
[0055] use as image 3 The shown non-water-soluble VOCs waste gas treatment process has a concentration of 22000mg / m for a chemical company 3 The exhaust gas of butyl butyrate (the air volume is 200m 3 / h) for processing, the specific process is as follows:
[0056] In this example, the water-insoluble VOCs specifically refers to butyl butyrate.
[0057]The exhaust gas treatment process containing butyl butyrate in this embodiment includes four exhaust gas absorption units arranged in series, namely, the head-end absorption tower 2, the second-stage absorption tower 3, the third-stage absorption tower 4 and the fourth-stage absorption tower 5. The absorbent enters the fourth-stage absorption tower 5, and the exhaust gas containing butyl butyrate enters from the head-end absorption tower 2, and cross-flow contacts with the absorbent in the head-end absorption tower 2, so that butyl butyrate is enriched in the absorbent Among them, in the present embodiment, the absorbent is ...
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