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

A process method and sulfur dioxide technology, applied in chemical instruments and methods, separation methods, dispersed particle separation, etc., can solve problems such as increased operating costs of devices, and the purity of sulfur products cannot meet market demand, etc. The effect of shortening and increasing the reaction rate

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

Examples

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Effect test

Embodiment 1

[0056] Process units for liquid phase 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; four gas inlet pipes 104-1, 104-2, 104-3 and 104-4 are arranged symmetrically on the reaction zone 102, as figure 2 As shown, all gas inlet pipes are arc-shaped pipes, and the radian and position of each gas inlet pipe are set so that the gas ejected is close to the center line of the reaction zone; the wall of the reaction zone 102 is also provided with a pH online monitor 105, the settling zone 103 is in an inverted conical shape, the bottom outlet of which...

Embodiment 2

[0058] A process device for reactive desulfurization of hydrogen sulfide and sulfur dioxide, such as image 3 As shown, the difference from the process device in Example 1 is that two gas inlet pipes 104-1 and 104-2 are arranged symmetrically on the reaction zone 102, as Figure 4 As shown, the gas inlet pipes 104-1 and 104-2 are a section of straight pipe + an arc pipe, and other structural settings are the same as those in Embodiment 1.

Embodiment 3

[0060] use figure 1 The processing method of hydrogen sulfide and sulfur dioxide reactive desulfurization in the shown process device is as follows:

[0061] Pure SO 2 The gas is passed into the reaction zone 102 of the reactor 100 through the gas inlet pipes 104-1 and 104-3, 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 through the gas inlet pipes 104-1 and 104-3, and is close to the center line of the reaction zone, driving the reaction solution in the reactor 100 to rotate, realizing the self-stirring effect of the liquid in the reactor 100, Good for 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 is passed through the gas inlet pipes 104-2 and 104-4, and the reaction solution ...

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Abstract

A process device and process method for liquid phase desulfurization of hydrogen sulfide and sulfur dioxide, including a reactor and a separator. Inlet pipe, which is arranged on the same level, and the gas inlet pipe extends to the inside of the reaction zone, which is an arc-shaped pipe, or a straight pipe whose end is bent into an arc-shaped; the settling area is connected to the separator, and the separator 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 can increase the dissolution rate and reaction rate of gas in the reaction solution, the response time of hydrogen sulfide and sulfur dioxide reaction is below 15s, the reaction conditions are mild, the obtained sulfur does not need to be refined, the purity is high, and the equipment is simple and easy to process , 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): B01D53/75B01D53/52B01D53/50B01D53/96B01D53/79
CPCB01D53/502B01D53/504B01D53/523B01D53/75B01D53/79B01D53/96B01D2251/80
Inventor 方向晨李磊王海波王明星金平齐慧敏韩天竹
Owner CHINA PETROLEUM & CHEM CORP
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