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Carbonyl sulfide hydrolysis catalyst and preparation method thereof

A hydrolysis catalyst, carbonyl sulfide technology, applied in chemical instruments and methods, physical/chemical process catalysts, separation methods, etc., can solve the problems of complex catalyst preparation process, high catalyst cost, low COS content in feed gas, etc. Effects of sulfation and anti-sulfur deposition functions

Inactive Publication Date: 2020-11-24
济南环陶环保工程有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] U.S. Patents USP4444987, USP4455446 and Chinese Patent CN102343271A disclose a catalyst that supports platinum sulfide on activated alumina. The disadvantage of this catalyst is that the cost of the catalyst is high, the COS content in the applicable raw material gas is low, and it needs to be regenerated regularly
[0004] Chinese patent CN108745338A discloses a magnesium-aluminum spinel medium-temperature carbonyl sulfide hydrolysis catalyst, which has the disadvantages of complex catalyst preparation process, high reaction temperature (above 300°C) and high energy consumption; Chinese patent CN106824149B uses polystyrene microspheres as macropores Template agent, using P123 as mesoporous template agent, using soluble titanium salt and soluble silicon as raw materials to synthesize a titania-based COS hydrolysis catalyst with an ordered pore structure with a large specific surface area, which can improve the sulfation resistance of the catalyst
The disadvantage is that the reaction temperature is 200-300 ° C, and there are certain requirements for the sulfur content in the raw material gas
Chinese patent CN100493699C discloses a medium temperature carbonyl sulfide hydrolysis catalyst K 2 O-V 2 o 5 - Aluminum oxide, which has good anti-oxidation properties, but its disadvantage is that the reaction temperature is high (200-400°C)

Method used

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preparation example Construction

[0032] The present invention also provides a preparation method for the carbonyl sulfide hydrolysis catalyst, comprising the steps of:

[0033] Step 1: Put gold chloride into deionized water and stir evenly;

[0034] Step 2: Add the catalyst to the mixed solution in Step 1, and stir evenly to obtain a suspension;

[0035] Step 3: drying the suspension obtained in Step 2 to obtain Intermediate 1;

[0036] Step 4: Roasting Intermediate 1 obtained in Step 3 to obtain Intermediate 2;

[0037] Step 5: using hydrogen to reduce the intermediate 2 obtained in step 4 to obtain intermediate 3;

[0038] Step 6: Add the alkali metal compound or alkaline earth metal into deionized water, pour the intermediate 3 prepared in step 5, and stir for 25-35 minutes to obtain intermediate 4;

[0039] Step 7: drying the intermediate 4 obtained in step 6 to obtain a carbonyl sulfide hydrolysis catalyst.

[0040] The drying temperature in step 3) is 40-150° C., and the drying time is 15 hours.

...

Embodiment 1

[0045] Weigh 1g of gold chloride and dissolve it in 10ml of deionized water, add 20g of aluminum oxide and stir evenly to obtain a gold chloride / aluminum oxide wet material; reduce with hydrogen at 250-350°C for 3 hours, and dry at 40-150°C 10 hours, roasting at 300-400°C for 5 hours in an air atmosphere to obtain the catalyst semi-finished gold / aluminum oxide; weigh 5g of sodium borohydride and dissolve it in 50ml deionized water, pour the catalyst semi-finished gold / aluminum oxide into the Stir for 30 minutes, and dry at 40-150° C. for 20 hours to obtain catalyst A.

Embodiment 2

[0047] Weigh 0.6g of gold chloride and dissolve it in 10ml of deionized water, add 30g of titanium dioxide and stir evenly to obtain a gold chloride / titanium dioxide wet material; dry the above wet material at 40-150°C for 15 hours, and then roast it in an air atmosphere at 300-400°C 5 hours, at 250-350 ℃ with hydrogen reduction for 3 hours, to obtain catalyst semi-finished gold / titanium dioxide; weigh 1.5g sodium carbonate and dissolve it in 15ml deionized water, then pour the above catalyst semi-finished gold / titanium dioxide, stir for 30min, Dry at -150°C for 15 hours to obtain catalyst B.

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Abstract

The invention discloses a carbonyl sulfide hydrolysis catalyst. The carbonyl sulfide hydrolysis catalyst comprises the following components in parts by weight: 0.001-10 parts of gold chloride, 0.001-10 parts of silver nitrate, 0.1-25 parts of an alkali metal compound, 0.1-25 parts of an alkaline earth metal compound, 65-99 parts of a catalyst and 0.01-100 parts of deionized water. The invention belongs to the technical field of catalysts for removing organic sulfur, and particularly relates to the carbonyl sulfide hydrolysis catalyst and a preparation method thereof. The purpose is achieved byadopting bifunctional active component. The catalyst is suitable for a wide temperature range from a low temperature (20 DEG C) to a medium temperature (400 DEG C), has no special limitation on the sulfur content in the raw material, can maintain long-term catalytic activity in the range of oxygen content of 5% in the raw material gas, and has relatively good sulfation resistance and sulfur deposition resistance functions.

Description

technical field [0001] The invention belongs to the technical field of catalysts for removing organic sulfur, and specifically refers to a carbonyl sulfide hydrolysis catalyst and a preparation method thereof. Background technique [0002] Carbonyl sulfide (COS) widely exists in synthesis gas with coal, coke, and heavy oil as raw materials, and also in coke oven gas in the coking industry and blast furnace gas in the iron and steel industry. Its existence has caused poison to downstream catalysts in the production process, and affected the performance of downstream catalysts. In addition, when coke oven gas and blast furnace gas are used as combustion gas, it also causes problems of equipment corrosion and environmental pollution. COS hydrolysis is the most practical way to remove organic sulfur, it is through the following reaction under the action of carbonyl sulfide hydrolysis catalyst: COS+hour 2 O → hour 2 S+CO 2 , convert COS into easily removed inorganic sulfides ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/52B01J23/66B01D53/86B01D53/48
CPCB01J23/52B01J23/66B01D53/8606
Inventor 程磊于波林光章于灏涵刘剑忠于涛王庆亭王腾王星
Owner 济南环陶环保工程有限公司
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