A process device and process method for reactive desulfurization of hydrogen sulfide and sulfur dioxide

A process method, sulfur dioxide technology, applied in chemical instruments and methods, separation methods, sulfur preparation/purification, etc., can solve the problems of sulfur product purity that cannot meet market demand, increase device operating costs, etc., to increase dissolution rate and reaction The effect of speed, prevention of deposition and scaling, and avoidance of coagulation and agglomeration

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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  • A process device and process method for reactive desulfurization of hydrogen sulfide and sulfur dioxide
  • A process device and process method for reactive desulfurization of hydrogen sulfide and sulfur dioxide
  • A process device and process method for reactive desulfurization of hydrogen sulfide and sulfur dioxide

Examples

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Embodiment 1

[0055] A process device for reactive desulfurization of hydrogen sulfide and sulfur dioxide, such as figure 1 As shown, the reactor 100 and the separator 200 are included, and the reactor is followed by the tail gas absorption zone 101, the reaction zone 102, and the settling zone 103 from top to bottom; the diameter ratio of the tail gas absorption zone 101 and the reaction zone 102 is 1:2 , the two are connected by a cone-shaped variable diameter. The tail gas absorption zone 101 is equipped with a solid tongue tray; two gas inlet pipes 104-1 and 104-2 are symmetrically arranged on the outer shell of the reaction zone 102, as figure 2 As shown, the gas inlet pipes 104-1 and 104-2 communicate with the reaction zone 102, and each gas inlet pipe is tangent to the peripheral wall of the reactor shell to form a snail shell; the wall of the reaction zone 102 is also provided with pH on-line monitor 105, the settling zone 103 is in an inverted conical shape, the bottom outlet is ...

Embodiment 2

[0057] A process device for reactive desulfurization of hydrogen sulfide and sulfur dioxide, such as image 3 As shown, different from the process device in Example 1, three gas inlet pipes 104-1, 104-2 and 104-3 are evenly distributed on the outer casing of the reaction zone 102, as Figure 4 As shown, other structural settings are the same as in Embodiment 1.

Embodiment 3

[0059] use figure 1 The processing method of hydrogen sulfide and sulfur dioxide reactive desulfurization in the shown process device is as follows:

[0060] Pure SO 2 The gas is passed into the reaction zone 102 of the reactor 100 through the gas inlet pipe 104-1, and the aqueous solution of the organic basic compound is housed in the reactor 100 as the reaction solution, SO 2 The gas enters the reaction zone 102 in a tangential direction after passing through the gas inlet pipe 104-1, driving the reaction solution in the reactor 100 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 solvent, 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 is passed into the tangential direction through the gas inlet pipe 104-2, and the liquid in the reaction zone 102 q...

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Abstract

A process device and process method for reactive desulfurization of hydrogen sulfide and sulfur dioxide, including a reactor and a separator. Gas inlet pipes, all gas inlet pipes are arranged on the same level, each gas inlet pipe is tangent to the wall of the reactor shell and connected to the cavity of the reaction zone, forming a snail shell shape; the settling zone is connected to the separator, and the separator’s The other end is connected to the top of the tail gas absorption zone of the reactor. 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 realize the effect of self-stirring of the solution in the reactor, which can increase the dissolution rate and reaction rate of the gas in the solvent, the response time of hydrogen sulfide and sulfur dioxide reaction is below 15s, the reaction conditions are mild, and the obtained sulfur does not need Refined, high purity, simple equipment, easy processing, low investment, safe operation.

Description

technical field [0001] The invention relates to a process device for 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 processes, a lar...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D53/78B01D53/50B01D53/52C01B17/05
CPCB01D53/523B01D53/78B01D2251/80C01B17/05
Inventor 何佳李磊方向晨齐慧敏王海波金平王明星
Owner CHINA PETROLEUM & CHEM CORP
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