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

A process method, sulfur dioxide technology, applied in chemical instruments and methods, separation methods, preparation/purification of sulfur, etc., can solve the problems that the purity of sulfur products cannot meet the market demand, increase the operating cost of the device, etc., shorten the reaction time, prevent Effect of depositing scale and increasing 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 reaction desulfurization of sulfur dioxide and hydrogen sulfide

Examples

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Effect test

Embodiment 1

[0056] Process devices for liquid-phase reaction desulfurization of sulfur dioxide and hydrogen sulfide, such as figure 1 As shown, it includes a reactor 10 and a separator 20. The reactor 10 is followed by a tail gas absorption area 100, a liquid holding tank area 200 and a reaction area 300 from top to bottom; the liquid holding tank area 200 includes a partition 201, Several gas lift cylinders 202 and downcomers 203, the partition plate 201 is fixed on the wall of the device to isolate the tail gas absorption zone 200 and the reaction zone 300, the gas lift cylinder 202 penetrates through the partition plate 201 and communicates with the tail gas absorption zone 100 and the reaction zone 300; one end of the downcomer 203 is fixed to the partition plate 201 and communicated with the exhaust gas absorption zone 100, and the other end extends downward to the bottom of the reaction zone 300; the lower part of the reaction zone 300 is provided with two nozzles 301, symmetrically ...

Embodiment 2

[0059] use figure 1 The process method for the reaction desulfurization of sulfur dioxide and hydrogen sulfide in the process unit shown is as follows:

[0060] First pure SO 2 The gas is introduced into the reaction zone 300 of the reactor 10 through the two nozzles 301. The reaction solution in the reaction zone 300 is an aqueous solution of an organic basic compound. When the pH online monitor 304 shows that it is 6.5, the gas starts to be passed into the reaction zone 300. pure H 2 S gas, the liquid in the reaction zone 300 quickly turns yellow, and it can be seen that the two react immediately to generate sulfur; the sulfur slurry flows upwards and enters the liquid collecting tank 302 under the impetus of the continuously introduced gas. When the liquid level is higher than the liquid phase, it is drawn out. When the outlet of the pipe 303, the slurry entrained with sulfur flows into the separator 20, and the sulfur and the reaction solution are separated, and the reac...

Embodiment 3

[0064] use figure 1 The process method for the reaction desulfurization of sulfur dioxide and hydrogen sulfide in the device shown:

[0065] Except that the organic alkaline compound aqueous solution is a 20% benzylamine solution, other conditions are the same as in Example 2.

[0066] Access H 2 The reaction response time of the two gases after S is 5s. According to the material balance calculation, H 2 The conversion rate of S was 93.7%.

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Abstract

The process device and process method of sulfur dioxide and hydrogen sulfide liquid phase reaction desulfurization, including reactor and separator, the reactor is followed by tail gas absorption area, liquid holding tank area and reaction area from top to bottom; liquid holding tank area includes partition, A number of lifters and downcomers are connected to the tail gas absorption area and the reaction area; at least two nozzles are arranged in the lower part of the reaction area, which are symmetrically distributed, and the nozzles are obliquely fixed on the wall of the reaction area, and the nozzles extend obliquely upward to the inside of the reaction area; The upper part of the reaction zone is provided with a liquid collection tank; the bottom of the liquid collection tank is provided with a liquid phase extraction pipe, which communicates with the liquid collection tank and the separator, and the other end of the separator is connected to the top of the tail gas absorption area. Using the process device of the present invention, the reaction gas is sprayed into the reactor through the nozzle and violently mixed with the reaction solution in the reactor, which greatly increases the dissolution rate and reaction rate of the gas in the reaction solution; the two symmetrical nozzles spray The gas reacts in the reaction solution to generate sulfur, and the gas that continues to be injected pushes the reaction solution entrained with sulfur to flow obliquely upward into the liquid collection tank. The solution in the reactor is always in a flowing state, preventing sulfur from depositing and scaling on the wall of the reactor and the bottom of the reactor, and ensuring the safe, stable and long-term operation of the device.

Description

technical field [0001] The invention relates to a process device for liquid-phase reaction desulfurization of sulfur dioxide and hydrogen sulfide, and a method for desulfurization by utilizing the process device, belonging to the field of industrial production or industrial waste gas purification. Background technique [0002] Due to the development of my country's economy, the demand for crude oil has increased unabated, and domestic crude oil is no longer enough to meet the national demand, so imported crude oil is being imported into China continuously. 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. As my country's imported crude oil increases 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 technologies. During cracking, catalytic cracking and other proc...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01D53/78B01D53/52B01D53/50C01B17/04
CPCB01D53/504B01D53/523B01D53/78B01D2251/80B01D2258/0283C01B17/04
Inventor 李磊王海波金平齐慧敏方向晨石平利刘炬王明星
Owner CHINA PETROLEUM & CHEM CORP
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