Method suitable for controlling concentration of hydrogen sulfide tail gas in low-temperature methanol washing process

A technology of low-temperature methanol washing and tail gas concentration, which is applied in chemical instruments and methods, separation methods, dispersed particle separation, etc., can solve problems such as the adverse effects of sulfur recovery operations, and achieve the effects of meeting environmental protection requirements, easy control, and simple operation.

Active Publication Date: 2015-03-25
SEDIN ENG
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AI Technical Summary

Problems solved by technology

The purified process gas is used in the post-process production, and the methanol solution that has absorbed impurity components such as carbon dioxide and hydrogen sulfide is recycled after decompression flashing, gas stripping, thermal regeneration and other regeneration processes, during which carbon dioxide is generated , sulfide exhaust tail gas, the acid tail gas containing hydrogen sulfide components should also be equipped with a sulfur recovery device to meet environmental protection requirements and recover sulfur or sulfuric acid and other by-products, but different sulfur recovery technologies have different requirements for the concentration of hydrogen sulfide in the tail gas , especially when the sulfur content in the raw gas varies greatly, fluctuations in the concentration of hydrogen sulfide in the sour tail gas will adversely affect the sulfur recovery operation

Method used

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  • Method suitable for controlling concentration of hydrogen sulfide tail gas in low-temperature methanol washing process

Examples

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Effect test

Embodiment 1

[0028] In this example 1, the sulfur-containing rich liquid 84m from the low-temperature methanol washing absorption unit 3 / h, temperature: -23°C, pressure: 3.52MPa, the specific composition is:

[0029] composition H 2 CO CO 2 CH 4 N 2 h 2 S COS CH 3 Oh ∑ wt% 0.01 0.20 24.46 19ppm 0.01 0.37 0.03 74.92 100.0

[0030] (1) Medium pressure flash evaporation

[0031] The sulfur-containing methanol-rich liquid from the low-temperature methanol washing gas purification and absorption unit, which has dissolved sulfide and carbon dioxide, first enters the medium-pressure flash tower 1 from the middle for decompression flash evaporation, the purpose of which is to remove the dissolved combustible gas in the solution through flash evaporation CH 4 , CO, H 2 Wait for the desorption to be recovered. The flash pressure is controlled in the range of 1.2MPa (Pa means absolute pressure), during which part of the H 2 S, CO 2 is also flas...

Embodiment 2

[0043] In this embodiment 2, the sulfur-containing rich liquid 182m from the low-temperature methanol washing absorption unit 3 / h, temperature: -20°C, pressure: 3.28MPa, the specific composition is:

[0044] composition H 2 CO CO 2 CH 4 N 2 h 2 S COS CH 3 Oh ∑ wt% 98ppm 0.20 20.9 155ppm 109ppm 0.70 0.12 78.08 100.0

[0045] In this embodiment, the process steps are the same as those in Embodiment 1. According to the change of raw material sulfur-rich liquid conditions, in order to meet the technological requirements of the sulfur recovery unit, some operating parameters will change as follows:

[0046] The flash pressure of medium pressure flash tower 1 is 0.75MPa;

[0047] The pressure in the reabsorption tower 2 is 0.19MPa;

[0048] The pressure of low-pressure nitrogen used for gas stripping is 0.4MPa;

[0049] The total sulfur (H 2 S+COS) content is 15.9% (v);

[0050] The temperature of the methanol-rich liquid en...

Embodiment 3

[0057] In this embodiment 3, 120m of sulfur-containing rich liquid from the low-temperature methanol wash absorption unit 3 / h, temperature: -27°C, pressure: 2.54MPa, the specific composition is:

[0058] composition H 2 CO CO 2 CH 4 N 2 h 2 S COS CH 3 Oh C 2 h 6 C 3 h 8 ∑ wt% 91ppm 0.1 20.5 0.1 72ppm 0.8 280ppm 78.0 557ppm 0.4 100.0

[0059] In this embodiment, the process steps are the same as in Embodiment 1. According to the change of raw material sulfur-rich liquid conditions, in order to meet the technological requirements of the sulfur recovery unit, some operating parameters will change as follows:

[0060] The flash pressure of medium pressure flash tower 1 is 0.6MPa;

[0061] The pressure in the reabsorption tower 2 is 0.15MPa;

[0062] The total sulfur (H 2 S+COS) content is 10.2% (v);

[0063] The temperature of the methanol-rich liquid entering the heat flash tank 8 is 77.5°C;

[0064] The flas...

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Abstract

The invention discloses a method suitable for controlling the concentration of hydrogen sulfide tail gas in a low-temperature methanol washing process. The method comprises the steps that a sulfur-bearing methanol rich solution dissolved with sulfide and carbon dioxide is subjected to flash evaporation via a medium-pressure flash evaporation tower; fuel gas such as CH4, CO and H2 dissolved in the solution is desorbed and recovered; the methanol solution after the flash evaporation is subjected to pressure reduction and gas stripping to allow a carbon dioxide component to be desorbed from the solution; sulfide is still dissolved in the methanol solution via secondary washing and absorption of the solution to achieve sulfide enrichment; the sulfur-bearing methanol rich solution is heated and then subjected to the flash evaporation; flash evaporation gas returns to a secondary absorption tower to strengthen the sulfide enrichment; the obtained sulfur-bearing methanol solution enters a heat regeneration tower to allow sulfide and residual CO2 to be fully desorbed by the action of steam stripping of methanol steam; and non-condensable gas, namely the acid sulfide tail gas is obtained by further condensation and cooling via a tail gas heat exchanger and a hydrogen sulfide tail gas chiller. The method has the advantages that the method is energy-saving and consumption-reducing, and can adapt to different sulfur recovery technology requirements.

Description

technical field [0001] The invention relates to a method suitable for controlling the concentration of hydrogen sulfide tail gas in the low-temperature methanol washing process. Background technique [0002] Low-temperature methanol washing process is widely used for desulfurization and decarbonation gas removal in the chemical production process. During the low-temperature methanol washing purification process, impurity components such as carbon dioxide and hydrogen sulfide in the raw process gas are washed and absorbed by methanol solvent to be removed. In addition to clean. The purified process gas is used in the post-process production, and the methanol solution that has absorbed impurity components such as carbon dioxide and hydrogen sulfide is recycled after decompression flashing, gas stripping, thermal regeneration and other regeneration processes, during which carbon dioxide is generated , sulfide exhaust tail gas, the acid tail gas containing hydrogen sulfide comp...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/14B01D3/06B01D3/38
CPCY02P70/10
Inventor 张琦宇李晓李刚尚书娟张凤娟王贵关杰刁秀辉
Owner SEDIN ENG
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