Treatment method for mixed organic waste gas containing chlorine, hydrogen chloride and oxynitride

A technology for nitrogen oxides and organic waste gas is applied in the treatment of hydrogen chloride and nitrogen oxides mixed organic waste gas and in the field of chlorine-containing gas. Treatment, achieving continuity and economic operational feasibility, effect to cover operating costs

Active Publication Date: 2016-05-25
NANJING TECH UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The general compound types are organic compounds such as hydrocarbons (alkanes, olefins and aromatics), ketones, esters, alcohols, phenols, aldehydes, amines, nitriles (cyanides), and there are various kinds of compounds in the above methods. For example, the main advantage of the catalytic combustion method is high purification efficiency and no secondary pollution. The problem is that the catalyst has high cost, short service life, difficult maintenance, and pretreatment is required when dealing with complex VOCs; the condensation method can only deal with high concentration, The range of gas flow is small, and the scope of use is relatively limited; adsorption or absorption methods generally use a large amount of adsorbent or absorption liquid, which is not only costly but also prone to secondary pollution
In many cases, adopting a purification technology is often difficult to meet the governance requirements, and it is not economical
From the content disclosed in the above prior art, it can be seen that there is no method for treating mixed waste gas containing chlorine, hydrogen chloride, nitrogen oxides and organic waste in the existing waste gas treatment methods, so it is necessary to develop a method for treating chlorine, hydrogen chloride, nitrogen oxides and A Simple, Practical and Economical Way to Mix VOCs in Exhaust Gas

Method used

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  • Treatment method for mixed organic waste gas containing chlorine, hydrogen chloride and oxynitride

Examples

Experimental program
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Effect test

Embodiment 1

[0050] 2,6-dichlorobenzonitrile is an intermediate of various herbicides and insecticides. The 2,6-dichlorobenzonitrile project of a factory produces chlorine gas and hydrogen chloride through chlorination, hydrolysis condensation, filtration, and rectification processes. , formic acid, nitric oxide, nitrogen dioxide, pyridine tail gas. Containing nitrogen oxides 56000mg / m 3 , Chlorine 68000mg / m 3 , hydrogen chloride 260000mg / m 3 , organic matter 8000mg / m 3 , exhaust gas at 500m 3 The flow rate per hour enters the condenser, the condensation temperature is 20°C, and the condensed waste gas enters the bottom of the first-stage packed tower, where the concentration of urea in the first packed tower is 15%, absorbing countercurrently with the waste gas from the bottom of the tower, and spraying Density is 50m 3 / m 2 h, the residence time of the waste gas is 18s, the absorption temperature is 50°C, the waste gas from the first packed tower enters the second packed tower from...

Embodiment 2

[0052] 2,4-Dichlorofluorobenzene is an intermediate in the synthesis of the broad-spectrum antibiotic ciprofloxacin. A company uses o-dichlorobenzene as raw material to synthesize 2,4-dichlorofluorobenzene through nitration, fluorination, chlorination, and rectification. The waste gas is mainly produced during the chlorination process, and its main components are chlorine, nitrogen oxides and Organic waste gas. Containing nitrogen oxides 3060mg / m 3 , Chlorine 7520mg / m 3 , hydrogen chloride 510mg / m 3 , organic waste gas 700mg / m 3 , exhaust gas at 200m 3 The flow rate of / h enters the condenser, the condensation temperature is 5°C, and the condensed exhaust gas enters the bottom of the first-stage packed tower. The urea concentration in the first packed tower is 10%, and it absorbs countercurrently with the tail gas from the bottom of the tower and sprays it. Density is 18m 3 / m 2 h, the waste gas residence time is 8s, the absorption temperature is 40°C, the tower diamete...

Embodiment 3

[0054] 1,2,4-Trichlorobenzene is an organic intermediate with a wide range of uses. It can be used not only as a solvent, but also as a raw material for the synthesis of medicines and pigments. A company uses 2,4-dinitrochlorobenzene to synthesize 1,2,4-trichlorobenzene by chlorination. During the synthesis process, there will be unreacted chlorine, nitrogen oxides and organic waste gas. Containing nitrogen oxides 4180mg / m 3 , Chlorine 6230mg / m 3 , hydrogen chloride 1620mg / m 3 , organic waste gas 4460mg / m 3 , exhaust gas at 100m 3 The flow rate of / h enters the condenser, the condensation temperature is 0°C, and the condensed exhaust gas enters the bottom of the first-stage packed tower. The urea concentration in the first packed tower is 10%, and it is absorbed countercurrently with the tail gas from the bottom of the tower and sprayed. Density is 24m 3 / m 2 h, the waste gas residence time is 11s, the absorption temperature is 45°C, the diameter of the packed tower is 0...

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Abstract

The invention discloses a treatment method for mixed organic waste gas containing chlorine, hydrogen chloride and oxynitride. The method is capable of not only achieving a favorable removal effect on oxynitride, but also achieving a favorable removal effect on chlorine. A condensation unit, an absorbing unit and an adsorption unit are adopted in the treatment method, wherein the condensation unit adopts one-grade condensation; the absorbing unit adopts four-grade absorption; the absorption unit adopts two-grade absorption; waste gas firstly passes through a cooler and a demister of the condensation unit, so that VOCs with relatively high boiling points in the waste gas are cooled as much as possible and then recycled; then the waste gas enters into an aqueous urea solution absorption tower of the absorbing unit, and nitric oxides and chlorine in the waste gas are completely oxidized, reduced, decomposed and absorbed by virtue of a catalytic absorption reaction, so that nitrogen and chlorine are removed; the waste gas with nitrogen and chlorine removal enters into an aqueous falling film solution absorption tower of the absorbing unit, so that by-product hydrochloric acid is obtained; finally, the residual waste gas passes through an absorption tower of the absorption unit, so that the residual VOCs are adsorbed, and thus up-to-standard release is achieved.

Description

technical field [0001] The invention relates to a treatment method for organic waste gas, more specifically to a treatment method for mixed organic waste gas containing chlorine, hydrogen chloride and nitrogen oxides. Background technique [0002] In pharmaceutical chemical, pesticide chemical, fine chemical and petrochemical industries, chlorination and nitration reactions are widely used to produce important chemical products. During the production process, a large amount of organic waste gas (VOCs) containing hydrogen chloride, chlorine, nitrogen oxides, etc. will be generated. ). These waste gases are more difficult to deal with than ordinary VOCs and are more harmful. On the one hand, there are many types of VOCs and complex components; on the other hand, the treatment of chlorine and nitrogen oxides is very troublesome and harmful. If not handled properly, light It will seriously pollute the environment, and seriously, personal injury and death accidents will occur, c...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/86B01D53/78B01D53/56B01D53/68
CPCB01D53/002B01D53/04B01D53/14B01D53/78B01D53/8625B01D53/8659B01D2251/2067B01D2253/102B01D2257/20B01D2257/404B01D2257/708Y02A50/20
Inventor 刘定华陈壮顾乃亚李松跃张汉杰刘晓勤孙林兵
Owner NANJING TECH UNIV
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