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Method for reducing concentration of carbonyl sulfide on outlet of hydrogen sulfide (H2S) desulfurizer

A technology of desulfurization agent and hydrogen sulfide, applied in chemical instruments and methods, separation methods, separation of dispersed particles, etc., to achieve high H2S removal rate, considerable economic and social benefits

Inactive Publication Date: 2010-08-11
TAIYUAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] The invention discloses a method for reducing the concentration of carbonyl sulfide at the outlet of a hydrogen sulfide desulfurization agent, the purpose of which is to solve the problem of desulfurization of the desulfurizer during the dry desulfurization process and improve the desulfurization performance of the desulfurizer, and discloses a method for reducing the outlet of the hydrogen sulfide desulfurization agent during the dry desulfurization process Technical scheme of the method for carbonyl sulfide concentration

Method used

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  • Method for reducing concentration of carbonyl sulfide on outlet of hydrogen sulfide (H2S) desulfurizer
  • Method for reducing concentration of carbonyl sulfide on outlet of hydrogen sulfide (H2S) desulfurizer

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Embodiment approach 1

[0031] Take by weighing about 112g of basic zinc carbonate, add 13g of potassium carbonate in basic zinc carbonate and mix evenly, then add about 9.5g of pseudo-boehmite in basic zinc carbonate and potassium carbonate mixture, and finally add about 3.75g of carboxymethyl cellulose and 0.25g of graphite mixture, mix all raw materials, add deionized water, knead and extrude at room temperature to obtain particles with a size of φ2~3mm×3~5mm, and place at room temperature for 24 hours Finally, dry at 120°C for 4 hours, and then bake the dried sample at 550°C for 4 hours to obtain a medium temperature zinc oxide desulfurizer. The desulfurizer is used at a temperature of 300°C and a space velocity of 2000h -1 , Import gas composition: 30Vol.% CO, 20Vol.% CO 2 , 40Vol.%H 2 , 1Vol.%H 2 O, N 2 balance, import H 2 S concentration is less than 300mgS / m 3 Under the condition, the measured exit H 2 S concentration and outlet COS concentration are both less than 0.1mgS / m 3 At this ...

Embodiment approach 2

[0033] Take by weighing about 119g of basic zinc carbonate, add 10g of potassium carbonate in basic zinc carbonate and mix evenly, then add about 7g of pseudo-boehmite in basic zinc carbonate and potassium carbonate mixture, and finally add 5.4 g of carboxymethyl cellulose and 0.36g of graphite mixture, mix all raw materials, add deionized water, knead and extrude at room temperature to obtain particles with a size of φ2~3mm×3~5mm, after standing at room temperature for 24 hours , dried at 120°C for 4 hours, and the dried sample was roasted at 550°C for 4 hours to obtain a medium temperature zinc oxide desulfurizer. The desulfurizer is used at a temperature of 300°C and a space velocity of 2000h -1 , Import gas composition: 30Vol.% CO, 20Vol.% CO 2 , 40Vol.%H 2 , 1Vol.%H 2 O, N 2 balance, import H 2 S concentration is less than 300mgS / m 3 , the measured outlet H 2 S concentration and outlet COS concentration are both less than 0.1mgS / m 3 At this time, the breakthrough ...

Embodiment approach 3

[0035] Take by weighing about 126g of basic zinc carbonate, add 7g of potassium carbonate in basic zinc carbonate and mix evenly, then add about 4g of pseudo-boehmite in basic zinc carbonate and potassium carbonate mixture, and finally add 7.5 g of carboxymethyl cellulose and 0.5 g of graphite mixture, mix all the raw materials, add deionized water, knead and extrude at room temperature to obtain particles with a size of φ2~3mm×3~5mm, after standing at room temperature for 24 hours , dried at 120°C for 4 hours, and the dried sample was roasted at 550°C for 4 hours to obtain a medium temperature zinc oxide desulfurizer. The temperature of the desulfurizer is 300°C, and the inlet gas composition: 30Vol.%CO, 20Vol.%CO 2 , 40Vol.%H 2 , 1Vol.%H 2 O, N 2 balance, import H 2 S concentration is less than 300mgS / m 3 , the measured outlet H 2 S concentration and outlet COS concentration are both less than 0.1mgS / m 3 At this time, the breakthrough sulfur capacity of the desulfuriz...

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Abstract

The invention provides a method for preparing hydrogen sulfide desulfurizer with dry process, in particular to a method for reducing the concentration of carbonyl sulfide on the outlet of the hydrogen sulfide (H2S) desulfurizer, belonging to the filed of the preparation and the application of the desulfurizer. The invention is characterized in that the desulfurizer which has high H2S desulfurizing rate and can reduce the concentration of carbonyl sulfide on the outlet of the H2S at moderate temperature is prepared by adding desulfurizer alkaline modifier K2CO3 to modify the alkaline of the desulfurizer and adding desulfurizer pore structure modifier Gamma-Al2O3 to modify the pore structure of the desulfurizer. The invention solves the problem existing in the prior art that a large amount of carbonyl sulfide is left on the outlet of the desulfurizer when the desulfurizer is used for desulfurizeing with dry process at moderate temperature. The invention is provided mainly for desulfurizing and purifying the H2S in the gases containing the carbon monoxide, the carbon dioxide and the like and has very considerable applicable, economic and social benefits.

Description

technical field [0001] The invention relates to a method for reducing the concentration of carbonyl sulfide at the outlet of a hydrogen sulfide desulfurizer, which belongs to the field of desulfurizer preparation and application, and relates to a method for preparing a dry-process hydrogen sulfide desulfurizer, specifically a method for reducing the medium temperature in the dry-process desulfurization process A zinc oxide-based hydrogen sulfide desulfurizer outlet carbonyl sulfide concentration method, the desulfurizer prepared by the method is mainly used for the removal of hydrogen sulfide in raw material gases containing carbon monoxide, carbon dioxide and the like. Background technique [0002] The rapid development of world industry and economy has led to tight energy supply and prominent environmental problems. All countries in the world are adopting active and corresponding policies to alleviate the contradictions between energy supply and demand, energy use and envi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01D53/86B01D53/48
Inventor 上官炬赵有生樊惠玲梁丽彤沈芳苗茂谦
Owner TAIYUAN UNIV OF TECH