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Process device and process method for liquid phase reaction desulfurization of hydrogen sulfide and sulfur dioxide

A process method, sulfur dioxide technology, applied in chemical instruments and methods, separation methods, preparation/purification of sulfur, etc., can solve the problems of increased operating costs of the device, and the purity of sulfur products cannot meet market demand, etc., to prevent deposition and scaling, Effects of increasing dissolution rate and reaction rate, and operating safety

Active Publication Date: 2021-07-09
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0015] In the above disclosed patents, H 2 S and SO 2 The pressure, temperature and pH value required for the reaction in pure water are very harsh. The reaction in an organic solvent or aqueous solution requires the addition of a buffer solution or catalyst to keep the organic solvent or aqueous solution acidic. The stronger the acidity (the lower the pH value) ) is more conducive to the reaction. During the operation of the device, the buffer solution or catalyst needs to be regularly replenished to maintain the acidic conditions required for the reaction, so the operating cost of the device increases; because the obtained liquid phase sulfur solution contains buffer solution or catalyst, the sulfur product The purity cannot meet the market demand, so sulfur refining equipment is needed to improve the purity of sulfur products

Method used

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  • Process device and process method for liquid phase reaction desulfurization of hydrogen sulfide and sulfur dioxide
  • Process device and process method for liquid phase reaction desulfurization of hydrogen sulfide and sulfur dioxide

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Embodiment 1

[0053] Hydrogen sulfide and sulfur dioxide liquid phase reaction desulfurization process equipment, such as figure 1 Shown, comprise reactor 100 and separator 200, described reactor 100 is followed by tail gas absorption zone 101, reaction zone 102, settling zone 103 from top to bottom; The diameter ratio of tail gas absorption zone 101 and reaction zone 102 is 1: 2. The two are connected through a cone-shaped variable diameter. Floating valve tray is housed in tail gas absorption zone 101; Said reaction zone 102 is provided with gas pipe 104, and it is fixed on the reactor 100, and described gas pipe 104 is made up of gas main pipe 1041 and gas branch pipe 1042, and described gas main pipe 1041 is a T-shaped tube composed of supervisor I 1041-1 and supervisor II 1041-2. The supervisor I 1041-1 opens on the wall of the reaction zone 102, extends horizontally to the center of the reactor 100 and communicates with supervisor II 1041-2, supervisor II 1041-2 Set in the center of ...

Embodiment 2

[0055] use figure 1 The processing method of hydrogen sulfide and sulfur dioxide reactive desulfurization in the shown process device is as follows:

[0056] Pure SO 2 The gas is passed into the reaction zone 102 of the reactor 100 through the gas pipe 104, and the gas is sprayed into the reaction solution in the reaction zone through the main pipe I 1041-1 and the main pipe II 1041-2 in turn through the gas branch pipe 1042. The reaction solution is an organic basic compound. The aqueous solution drives the reaction solution to rotate, realizing the effect of self-stirring of the liquid in the reactor, which is beneficial to SO 2 Uniform dispersion of gas in the reaction solution, and greatly increased SO 2 The dissolution rate of the gas in the reaction solution, when the pH online monitor 105 shows 6.5, start to feed pure H into the reaction zone 102 2 S gas, the liquid in the reaction zone 102 turns yellow quickly, and it can be seen that the two react immediately to ge...

Embodiment 3

[0060] use figure 1 The process method for hydrogen sulfide and sulfur dioxide reactive desulfurization in the shown device:

[0061] Except that the organic alkaline compound aqueous solution is 20% benzylamine solution, other conditions are the same as embodiment 2.

[0062] Access to H 2 The reaction response time of the two gases after S is 5s, calculated according to the material balance, H 2 The conversion rate of S was 94.9%.

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Abstract

A process device and process method for hydrogen sulfide and sulfur dioxide liquid-phase reaction desulfurization, including a reactor and a separator. The other end of the reactor is connected to the top of the tail gas absorption area of ​​the reactor; the reaction area is provided with a gas pipe, which is composed of a main gas pipe and a gas branch pipe, and the pipes in the gas pipe are connected to each other, and the two ends of the main pipe II are closed. The hydrogen sulfide and sulfur dioxide desulfurization reaction is carried out by using the above-mentioned device, and the reaction solution includes water and at least one organic basic compound that can dissolve in water, so that the pH value of the solution is ≥ 7.2. The device and method of the present invention can make the reaction gas entering the reactor form a spray with a certain arc, promote the self-stirring of the liquid, facilitate the uniform dispersion of the gas in the reaction solution, and greatly increase the concentration of the gas in the reaction solution. Dissolution rate and reaction rate; the reaction time of hydrogen sulfide and sulfur dioxide is less than 15s, the reaction conditions are mild, the obtained sulfur does not need to be refined, the purity is high, the equipment is simple and easy to process, the investment is low, and the operation is safe.

Description

technical field [0001] The invention relates to a process device for liquid-phase reaction desulfurization of hydrogen sulfide and sulfur dioxide, and a desulfurization method using the process device, belonging to the field of industrial production or industrial waste gas purification. Background technique [0002] Due to the development of our country's economy, the demand for crude oil continues to increase, and domestic crude oil is no longer enough to meet national needs, so imported crude oil is continuously being imported into China. From January to December 2016, China imported 381.01 million tons of crude oil, an increase of 13.6% compared with the same period last year. With the increase of my country's imported crude oil year by year, the proportion of high-sulfur crude oil is increasing. For this reason, major oil refining companies have developed a series of high-sulfur crude oil processing technology. During cracking, catalytic cracking and other processing pro...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D53/78B01D53/52C01B17/04
CPCB01D53/1418B01D53/1468B01D53/1481B01D53/1493B01D53/18B01D53/523B01D53/78B01D2252/204C01B17/04
Inventor 李磊齐慧敏王海波金平方向晨刘炬石平利王昊辰
Owner CHINA PETROLEUM & CHEM CORP
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