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Method for preparing clean CO sulfur tolerant shift catalyst

A sulfur-resistant shift and catalyst technology, which is applied in catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of low strength stability, poor hydration resistance, short service life, etc. The effect of good stability, solving pollution problems and low loss rate of active components

Active Publication Date: 2013-01-02
CHINA PETROLEUM & CHEM CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although these technologies also use clean raw materials for catalyst preparation, the carrier is basically γ-Al 2 o 3 Type, poor hydration resistance, low strength stability, short service life, can only be used in limited process conditions, low promotion and application value

Method used

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  • Method for preparing clean CO sulfur tolerant shift catalyst
  • Method for preparing clean CO sulfur tolerant shift catalyst
  • Method for preparing clean CO sulfur tolerant shift catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] First dissolve 300g magnesium acetate in 500ml deionized water and 80g Al 2 O3 Fully mixed with 25g of metatitanic acid, dried, and roasted at 500 ° C for 4 hours; the roasted material (basic material A, the same for other embodiments) was pulverized through a 200-mesh sieve, and 100 g of powder (basic material A, other Example same), 170g Al(OH) 3 , 30g MgO, 15g metatitanic acid were mixed, the solution made of 8g acetic acid and 150ml deionized water was added for kneading, molding, and the catalyst carrier was obtained by calcining at 550 ° C for 3 hours after natural drying.

[0035] Take 100g of carrier, mix 15g of ammonium molybdate, 8.0g of cobalt acetate, 6.0g of potassium carbonate and 50ml of deionized water into a co-dipping solution, immerse the dipping solution in equal volume, dry it at 120°C, and decompose it at 500°C. The finished catalyst (catalyst number is C-1), its strength and strength stability are shown in Table 1.

Embodiment 2

[0037] First, 300g of magnesium acetate was dissolved in 500ml of deionized water, 110g of pseudo-boehmite and 20g of zinc oxide were fully mixed, dried, and roasted at 550 ° C for 4 hours. , 200g

[0038] Al 2 O 3 , 30g MgO, 10g titanium oxide are mixed, add the solution made up of 8g citric acid and 150ml deionized water for kneading, molding, after natural drying, calcination at 550 ℃ for 3 hours to obtain the catalyst carrier.

[0039] Take 100g of carrier, mix 15g of ammonium molybdate, 8.0g of cobalt acetate, 5.0g of potassium hydroxide and 50ml of deionized water into a co-dipping solution, immerse the dipping solution in equal volume, dry it at 120°C, and decompose it at 500°C. The finished catalyst (catalyst number is C-2) is obtained, and its strength and strength stability are shown in Table 1.

Embodiment 3

[0041] First, 300g of magnesium acetate was dissolved in 500ml of deionized water, 110g of pseudo-boehmite and 20g of titanium oxide were fully mixed, dried, and roasted at 500 ° C for 4 hours. , 200gAl 2 O 3 , 35g of magnesium hydroxide, 10g of titanium oxide were mixed, and a solution of 5g of citric acid, 5g of oxalic acid and 160ml of deionized water was added for kneading, molding and calcining at 550 ° C for 3 hours to obtain a catalyst carrier.

[0042] Take 100g of carrier, mix 15g of ammonium molybdate, 10.0g of cobalt oxalate, 5.0g of potassium hydroxide and 50ml of deionized water into a co-dipping solution, immerse the dipping solution in equal volume, dry it at 120°C, and decompose it at 500°C. The finished catalyst (catalyst number is C-3) is obtained, and its strength and strength stability are shown in Table 1.

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Abstract

The invention provides a method for preparing a clean CO sulfur tolerant shift catalyst. The mode of adding active ingredients and an alkali metal aid is optimized, the active ingredients are high in dispersibility on the surface of a carrier and difficult to lose, and the catalyst is prepared by an immersion method and also can be directly prepared by a kneading method. The preparation method issimple and practicable; and the prepared clean CO sulfur tolerant shift catalyst has higher strength, strength stability and structural stability; the wastage rate of the active ingredients is low, the activity stability is high, the catalyst has high capacity of resisting poisonous substances such as carbonyl iron, and the physicochemical properties meet industrial requirement. In the process ofpreparing the catalyst, pollutant gases such as nitric oxides are not generated, and the cleanliness and environmental friendliness are achieved.

Description

technical field [0001] The invention relates to a preparation method of a clean CO sulfur-tolerant shift catalyst used for the shift reaction of sulfur-containing CO gas and water vapor. Background technique [0002] Restricted by oil and natural gas resources, most nitrogen fertilizer plants, methanol plants and coal chemical plants in my country use coal or residual oil as raw materials, pressurized gasification to generate gas, followed by carbon monoxide and sulfur-resistant transformation. Shift catalyst. According to the different operating pressure of the shift system, the sulfur-resistant shift process in my country can be roughly divided into several different processes: high pressure (>6.0MPa), medium pressure (2.0-5.0MPa), and low pressure (<2.0MPa). Among them, the medium-pressure sulfur-resistant shift process is the most complex, including the advanced Texaco coal-water slurry gasification and Luqi coal pressurized gasification process. In addition, ther...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/882B01J37/02B01J37/04C01B3/48C01B3/16
CPCY02P20/52
Inventor 白志敏余汉涛田兆明齐焕东陈依屏郭建学李文柱郭杰
Owner CHINA PETROLEUM & CHEM CORP