Three-stage countercurrent absorption process and apparatus for acidic gases

A three-stage countercurrent, acid gas technology, applied in inorganic chemistry, sulfur compounds, dispersed particle separation, etc., can solve the problems of difficult operation of the device, long process, easy deterioration of sodium sulfide, etc., to prevent crystallization and reduce the concentration of Na2S. Effect

Active Publication Date: 2015-08-12
CHINA PETROLEUM & CHEM CORP +1
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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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  • Three-stage countercurrent absorption process and apparatus for acidic gases

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Embodiment 1

[0055] use as figure 1 The process device shown uses acid gas and NaOH solution with a mass concentration of 35% as raw materials for 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%.

[0056] In the embodiment of the present invention, the primary reactor and the secondary reactor adopt rotary bed reactors, and the reaction temperature in the primary rotary bed reactor and the secondary rotary bed reactor is 85°C. The temperature of the primary intermediate tank and the secondary intermediate tank is 90°C. The rotational speed of the primary rotary bed reactor and the secondary rotary bed reactor is 1500 rpm. The residence time of the reaction materials in the reactor was 10 seconds.

[0057] In the process of the present invention, in step (1), the volume flow ratio of the reaction product liquid circulated back to the secondary intermediate tank and the total reaction product liquid o...

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Abstract

The invention discloses a three-stage countercurrent absorption process and apparatus for acidic gases. The absorption process 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 process, a supplementary carrier gas pipeline is arranged on a connection pipeline located between a gas phase outlet and an inlet of a two-stage rotating bed reactor to introduce a supplementary carrier gas, so the concentration of CO2 in the acidic gases is reduced; most CO2 is taken out of the apparatus; thus, the contents of Na2CO3 and NaHCO3 are controlled, obstruction of the pipelines due to crystallization caused by production of a great amount of Na2CO3 is prevented, and long cycle operation of the apparatus is guaranteed. The absorption process for acidic gases provided by the invention is simple and can achieve the dual objectives of purification of acidic gases and reclamation of pollutants; and an acidic gas treating system has the advantages of small scale, low energy consumption and low proneness to obstruction.

Description

technical field [0001] The invention relates to an acid gas absorption process and device, belonging to the field of acid gas purification, in particular to a treatment process and device suitable for the purification of sulfur-containing hydrogen acid gas and the recycling of pollutants. Background technique [0002] Refinery acid gas mainly comes from sour water stripping, circulating hydrogen desulfurization, dry gas desulfurization and other devices. The acid gas mainly contains H 2 S, CO 2 . At present, the acid gas in most small refineries basically adopts the treatment method of post-combustion emission. On the one hand, this method causes a waste of resources, on the other hand, it brings huge pressure to 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 acid gas in lar...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/78B01D53/52B01D53/62C01B17/32
Inventor 孟凡飞彭德强王璐瑶王岩陈新陈建兵王阳峰孟凡忠
Owner CHINA PETROLEUM & CHEM CORP
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