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

A technology for sulfur dioxide and process equipment, which is applied in chemical instruments and methods, separation methods, and dispersed particle separation, etc., can solve the problems that the purity of sulfur products cannot meet the market demand and increase the operating cost of the equipment, shorten the reaction time, and prevent the deposition and junction. Scaling, the effect of increasing the dissolution rate

Active Publication Date: 2019-03-29
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 of liquid phase desulfurization of hydrogen sulfide and sulfur dioxide
  • Process device and process method of liquid phase desulfurization of hydrogen sulfide and sulfur dioxide
  • Process device and process method of liquid phase desulfurization of hydrogen sulfide and sulfur dioxide

Examples

Experimental program
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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

Disclosed are a process device and a process method of liquid phase desulfurization of hydrogen sulfide and sulfur dioxide. The process device includes a reactor and a separator. The reactor includesa tail gas absorption zone, a reaction zone and a sedimentation zone. A shell of the reaction zone is provided with at least two gas inlet tubes which are arranged on the same horizontal plane. The gas inlet tubes extend to the inside of the reaction zone and are arc-shaped tubes or straight tubes with the ends being curved into an arc shape. The sedimentation zone is connected to the separator. The other end of the separator is connected to the top of the tail gas absorption zone of the reactor. The device is used for a desulfurization reaction of the hydrogen sulfide and sulfur dioxide, anda reaction solution includes water and at least one organic alkaline compound soluble in water so as to make the pH value of the solution greater than or equal to 7.2. The device and method of the invention can increase the dissolution rate and reaction rate of gas in the reaction solution. The respond time of the reaction of the hydrogen sulfide and sulfur dioxide is less than 15 s. The reactionconditions are mild, obtained sulfur does not need to be refined and is high in purity, the equipment is simple and easy in processing, the investment is low, and the operation is safe.

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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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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