Process for recovering benzene-containing tail gas from preparation of cis-butenedioic anhydride by benzene oxidation

A technology of benzene tail gas and maleic anhydride, which is applied in the field of adsorption and recovery of benzene in benzene tail gas, can solve problems such as low adsorption efficiency, waste of benzene resources, and increase environmental protection efforts, and improve the ability and purification efficiency, improve economic and social Benefit, low-cost adsorption treatment effect

Active Publication Date: 2009-10-28
QINGDAO HSJ ENVIRONMENTAL PROTECTION TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in the existing industrial VOCs waste gas recovery technology, the condensation recovery technology can only deal with small air volume and high concentration of VOCs waste gas; the adsorption recovery process uses adsorbents, and the saturated water vapor in the tail gas will cause VOCs components in the adsorbent bed. Rapidly penetrate through the layer, and the adsorption efficiency is very low, so it cannot be directly used for the recovery and reuse of useful VOCs components in this type of exhaust gas
At present, most domestic production enterprises using benzene oxidation method to produce maleic anhydride directly discharge without any treatment, which not only causes a lot of waste of benzene resources, but also causes serious environmental pollution, and also violates the relevant environmental protection laws and regulations of our country. Investment in pollution control, increasing environmental protection efforts, and building a harmonious society are incompatible with the environment

Method used

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  • Process for recovering benzene-containing tail gas from preparation of cis-butenedioic anhydride by benzene oxidation

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] combine figure 1 , the benzene-containing tail gas comes from the benzene oxidation unit, and the benzene vapor concentration in the tail gas is 1230mg / m 3 , Simultaneously because tail gas has passed through the water washing process of 60 ℃, tail gas is saturated by water vapor, and water vapor accounts for about 19.6% of whole tail gas composition (the water vapor content mentioned below is all by volume), and humidity is 100%. The tail gas is sent into the dehumidifier 2 by the first-stage adsorption fan 1, and the tail gas is first cooled to 24°C in the dehumidifier 2, and the water vapor content is 3%, which is still saturated; At this time, the water vapor content in the tail gas is still 3%, but the relative humidity drops to 40%. Then the dehumidified tail gas enters the primary adsorption tower 3 under the wind pressure of 0.11MPa, and the benzene in it is adsorbed by activated carbon, and the concentration of benzene vapor in the tail gas after the primary a...

Embodiment 2

[0026] The difference between this example and Example 1 is the benzene-containing tail gas saturated with water vapor at 60°C, wherein the concentration of benzene vapor is 1052 mg / m 3 , with a water content of 19.6%, the tail gas is first cooled to 18°C ​​in the dehumidifier 2, the water vapor content is reduced to 2%, and then the temperature is raised to 30°C, and the relative humidity is reduced to 45%. The tail gas after dehumidification enters the first-stage adsorption tower 3 under the wind pressure of 0.13MPa, and the benzene is adsorbed by activated carbon. The concentration of benzene vapor in the tail gas after the first-stage adsorption is 50mg / m 3 , the primary adsorption rate is about 95%; then the primary adsorption tail gas enters the secondary adsorption tower 4 to continue the adsorption, and the concentration of benzene in the discharged tail gas is only 10mg / m 3 , less than 12mg / m 3 The national secondary emission standard, can be discharged directly. W...

Embodiment 3

[0028] The difference between this example and Example 1 is that the tail gas has undergone a water washing process at 80°C, and the benzene concentration in the tail gas is 890 mg / m 3, the water content is as high as 46.8%. The tail gas is first cooled to 25°C in the dehumidifier 2, the water vapor content is reduced to 3%, and then the temperature is raised to 40°C, and the relative humidity is reduced to 40%. The tail gas after dehumidification enters the first-stage adsorption tower 3 under the wind pressure of 0.12MPa, and the benzene is adsorbed by activated carbon. The concentration of benzene vapor in the tail gas after the first-stage adsorption is 48mg / m 3 , the primary adsorption rate is about 95%; then the primary adsorption tail gas enters the secondary adsorption tower 4 to continue the adsorption, and the concentration of benzene in the discharged tail gas is only 9mg / m 3 , less than 12mg / m 3 The national secondary emission standard, can be discharged directly....

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Abstract

The invention discloses a process for recovering benzene-containing tail gas from the preparation of cis-butenedioic anhydride by benzene oxidation, which comprises the following steps that: after entering a dehumidifier to reduce liquid water content, a tail gas exhausted from a production device enters a primary absorption tower and passes through the primary absorption tower and a secondary absorption tower at 30 to 40 DEG C and 0.12 MPa, wherein the total adsorption rate of the primary absorption and secondary absorption can reach 99.7 percent and the total recovery rate of the primary absorption and the secondary absorption is up to 95 percent; the tail gas subjected to the secondary absorption has a benzene content less than the national discharge standard of 12mg / m and can be discharged directly; when the absorption rate of the absorption towers reach 90 percent, vapor at a high temperature of 110 DEG C introduced into the absorption tower for desorption, and desorbed benzene-containing vapor is subjected to condensation and gravity segregation to recover benzene; and when the absorption rate of the absorption towers reaches above 90 percent, the absorption towers are dried by introduced drying hot air and change into an absorption state again. The process has the advantages of achieving high benzene recovery rate, effectively recovering the benzene, creating considerable economic benefits, discharging the tail gas after the tail gas reaches the standard, and creating remarkable social benefits.

Description

technical field [0001] The invention relates to an adsorption and recovery process for benzene-containing tail gas, in particular to an adsorption and recovery process for benzene in benzene tail gas containing a large amount of saturated water vapor produced during the benzene oxidation process to produce maleic anhydride. Background technique [0002] Maleic anhydride, also known as maleic anhydride, chemically named maleic anhydride, is an important organic chemical raw material, the third largest anhydride after phthalic anhydride and acetic anhydride. At the end of 2007, the production capacity of maleic anhydride in my country was about 900,000 tons , by 2010, it will reach 1.3 million tons, and the market demand is large. Maleic anhydride is mainly used in the production of unsaturated polyesters and alkyd resins, and is also used in pesticides, paints, inks, lubricating oil additives, paper chemicals, textile finishing agents, surfactants and other fields. Maleic anh...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/04B01D53/26C07D307/60
CPCY02P20/50
Inventor 郅立鹏陈继朝王占义侯明霞朱本科
Owner QINGDAO HSJ ENVIRONMENTAL PROTECTION TECH CO LTD
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