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Acidic gas countercurrent absorption method and system

An acid gas, countercurrent technology, applied in separation methods, chemical instruments and methods, inorganic chemistry, etc., can solve the problems of difficult operation of the device, easy deterioration of sodium sulfide, and difficult promotion.

Active Publication Date: 2015-08-12
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] The two-stage Claus + tail gas hydrogenation reduction + solvent absorption technology has mature technology, stable operation, and stable product sulfur quality. However, due to the long process and large investment, the Claus process can only deal with high-concentration acid gases. 2 When the S volume fraction is less than 20%, the device is not easy to operate
This process can only produce 98% industrial sulfuric acid, but cannot produce oleum with higher value. At the same time, due to the difficulty in the transportation and storage of sulfuric acid, the stable market demand near the refinery is an important factor limiting its development.
[0009] CN1836767A discloses a treatment method for sour gas in refineries, utilizing sour gas as the fuel for shaft kilns in cement plants, when the sour gas is burned in the kiln, the H 2 S component reacts chemically with cement material to generate CaSO 4 , other harmful components are also sintered and transformed, which fundamentally solves the problem of acid gas treatment. At the same time, acid gas is used as a gas fuel to make the cement plant energy-saving fuel and achieve the dual purposes of environmental protection and fuel resolution. However, this The method has certain limitations and is not easy to promote
However, the sodium sulfide product of this process is prone to deterioration and is not easy to store

Method used

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  • Acidic gas countercurrent absorption method and system
  • Acidic gas countercurrent absorption method and system
  • Acidic gas countercurrent absorption method and system

Examples

Experimental program
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Effect test

Embodiment 1

[0076] using as figure 1 The shown process method and system use acid gas and NaOH solution as raw materials to carry out the reaction. CO in acid gas 2 The volume fraction is 7%, H 2 The volume fraction of S is 92%, and the volume fraction of hydrocarbons is 1%. The mass concentration of NaOH solution is 38%.

[0077] In Example 1, a Venturi reactor is used for the primary reactor and the secondary reactor, and a rotating bed reactor is used for the third-stage reactor and the fourth-stage reactor. The Venturi reactor and the rotating bed reactor can be in the art General purpose Venturi and rotating bed reactors.

[0078] In Example 1, the volume flow ratio of the second-path reaction product liquid recycled back to the primary reactor to the total reaction product liquid of the first-stage reactor was 5:6. The volume flow ratio of the second-path reaction product liquid recycled back to the secondary reactor to the total reaction product liquid of the second-stage reac...

Embodiment 2

[0082] using as figure 2 The process method and system shown, in Example 2, the primary reactor and the secondary reactor were image 3 The venturi, tertiary and quaternary reactors shown employ rotating bed reactors.

[0083] In Example 2, the volume flow ratio of the reaction product liquid circulated back to the first stage reactor through the absorption liquid inlet of the first stage reactor to the total reaction product liquid of the first stage reactor is 5:8. The volume flow ratio of the reaction product liquid circulating back to the first stage reactor through the circulating liquid inlet of the first stage reactor to the total reaction product liquid of the first stage reactor is 5:24.

[0084] The volume flow ratio of the reaction product liquid circulating back to the second stage reactor through the absorption liquid inlet of the second stage reactor and the total reaction product liquid of the second stage reactor is 5:8. The volume flow ratio of the reaction...

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Abstract

The invention provides an acidic gas countercurrent absorption method and system. The acidic gas absorption method employs a gas-liquid two-phase countercurrent absorption reaction and uses a NaOH solution as an absorption liquid to treat acidic gases so as to produce NaHS. According to the method, a crystallizer and a separator are arranged in a primary reaction and a secondary reaction, and heat is taken out of a reactor; and through filling of the NaOH solution in stages, peak clipping of reaction heat is realized, and local crystallization caused by generation of heat spots is prevented. A combination of a Venturi reactor and a rotating packed bed reactor is used as a reaction apparatus which is flexible to operate and has high mass transfer efficiency. The acidic gas countercurrent absorption method provided by the invention is simple and can achieve the dual objectives of purification of acidic gas and reclamation of pollutants; and the acidic gas countercurrent absorption system has the advantages of small scale, low energy consumption and low proneness to obstruction.

Description

technical field [0001] The invention provides a countercurrent absorption method and system for acid gas, belonging to the field of acid gas purification, in particular to a treatment method and system suitable for the purification of sulfur-containing hydride acid gas and the recycling of pollutants. Background technique [0002] Refinery sour gas mainly comes from sour water stripping, circulating hydrogen desulfurization, dry gas desulfurization and other devices, and the sour gas mainly contains H 2 S, CO 2 . At present, the acid gas of most small refineries basically adopts the treatment method of post-combustion emission. On the one hand, this method causes waste of resources, on the other hand, it brings huge pressure on environmental protection and affects the development space of enterprises. In order to protect the environment and ensure the full utilization of resources, it is imperative to recycle the acid gas from small refineries. [0003] The treatment of ...

Claims

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Application Information

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IPC IPC(8): B01D53/78B01D53/52B01D53/62B01D53/96C01B17/32
Inventor 齐慧敏李克见彭德强王璐瑶陈建兵孟凡飞陈新王岩
Owner CHINA PETROLEUM & CHEM CORP
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