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High space velocity sulfur resistant pre-shift catalyst and preparation method thereof

A catalyst and pre-conversion technology, applied in the direction of chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the effects of catalyst activity and activity stability, internal active components Decreased utilization rate, large influence of internal diffusion, etc., to achieve the effects of strong adsorption and removal of poisons, good conversion activity and activity stability, and high compressive strength

Active Publication Date: 2018-09-21
CHINA PETROLEUM & CHEM CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Due to the low gas space velocity of the conventional sulfur-tolerant shift catalyst, it is greatly affected by internal diffusion, and the active components of the catalyst are required to be evenly distributed to make the utilization rate high and prolong the service life of the catalyst; however, the pre-shift catalyst in the sulfur-tolerant pre-shift process When the service conditions change, the gas space velocity increases greatly, which is greatly affected by external diffusion, and when the gas space velocity reaches a certain value, the external diffusion influence dominates, and the sulfur-resistant pre-shift catalyst is still used in the preparation of the main shift catalyst. process, when the high air space velocity is affected by external diffusion, the utilization rate of the internal active components is greatly reduced, which affects the catalyst activity and activity stability to a certain extent

Method used

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  • High space velocity sulfur resistant pre-shift catalyst and preparation method thereof
  • High space velocity sulfur resistant pre-shift catalyst and preparation method thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0038] Dissolve 5.63 g of ammonium molybdate in 20 ml of deionized water, and adjust the pH to 7.5 with ethylenediamine to obtain solution A. Solution B was obtained by dissolving 7.90 g of nickel nitrate and 7.77 g of cobalt nitrate in 25 ml of deionized water. Then 3 g of citric acid and 4.3 g of metatungstic acid were dissolved in 10 ml of deionized water to obtain solution C. Mix 93g of pseudo-boehmite, 16.5g of light magnesium oxide, 14.3g of metatitanic acid, and 3g of Tianqing powder, add solution C, and knead evenly; use a 20-hole die to extrude into a honeycomb-like carrier, and dry naturally And 500 ℃ calcined to prepare the catalyst carrier. Put the calcined catalyst carrier in a weakly acidic solution adjusted to PH=6.5 with citric acid and oxalic acid, soak it at 40°C for 4 hours, take it out, dry it at 70°C for 2 hours, and then dry it at 220°C for 2 hours to get pretreated carrier; put the pretreated catalyst carrier into solution B for equal-volume impregnati...

Embodiment 2

[0049] Dissolve 5.63 g of ammonium molybdate with 15 ml of deionized water, and adjust the pH to 7.1 with triethanolamine to obtain solution A. Solution B was obtained by dissolving 1.95 g of nickel nitrate and 11.65 g of cobalt nitrate in 30 ml of deionized water. Then 2 g of acetic acid and 5.4 g of magnesium acetate were dissolved in 10 ml of deionized water to obtain solution C. Mix 60g of alumina, 20g of light magnesia, 12g of titanium oxide, 1g of sucrose and 2g of starch evenly, add solution C, and knead evenly; use a 16-hole die to extrude into a honeycomb-like carrier, naturally dry and roast at 450°C Then the catalyst carrier is prepared. Place the calcined catalyst carrier in a weakly acidic solution adjusted to PH=5.5 with citric acid, soak it at 35°C for 3 hours, take it out, dry it at 70°C for 2 hours, and then dry it at 220°C for 1 hour to get the pretreated carrier Put the pretreated catalyst carrier into solution B for equal volume impregnation for 2 hours, ...

Embodiment 3

[0051] 6.2 g of ammonium molybdate was dissolved in 20 ml of deionized water, and the pH was adjusted to 7.6 with propanolamine to obtain solution A. Solution B was obtained by dissolving 7.90 g of nickel nitrate and 3.9 g of cobalt nitrate in 25 ml of deionized water. Then 2 g of oxalic acid, 2 g of citric acid and 6.07 g of copper nitrate were dissolved in 15 ml of deionized water to form solution C. Mix 100g of aluminum glue, 27g of heavy magnesium oxide, 22g of metatitanic acid, and 4g of polyvinyl alcohol evenly, add solution C, and knead evenly; use a 14-hole die to extrude into a honeycomb-like carrier, naturally dry and bake at 600°C Then the catalyst carrier is prepared. Put the calcined catalyst carrier in a weakly acidic solution adjusted to PH=6.8 with oxalic acid and acetic acid, soak it at 30°C for 10 hours, take it out, dry it at 70°C for 5 hours, and then dry it at 220°C for 1 hour to get the pretreated Carrier: Put the pretreated catalyst carrier into soluti...

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Abstract

The invention relates to a catalyst and concretely relates to a high-air speed sulfur-resistant pre-shift catalyst. The sulfur-resistant pre-shift catalyst utilizes magnesium, aluminum and titanium composite carriers, utilizes molybdenum, cobalt and nickel as active components and one or more of tungsten oxide, iron oxide, manganese oxide, copper oxide and magnesium oxide as active component assistants. The catalyst has high compressive strength, a good structure and activity stability, has a strong toxin adsorption and removal capability, has a high active ingredient utilization rate and is not easily lost. The invention also provides a preparation method of the catalyst. The preparation method has reasonable processes. The catalyst still has good activity and activity stability under conditions of high air speed transformation and even under the condition of a higher air speed, has a long use period and can realize toxin and ash adsorption and removal.

Description

technical field [0001] The invention relates to a catalyst, in particular to a high space velocity sulfur-resistant pre-shift catalyst and a preparation method thereof. Background technique [0002] The purpose of the sulfur-tolerant pre-shift process is to pre-shift the process gas to reduce the burden on the subsequent shift system, reduce the impact on the subsequent main shift catalyst caused by the instability of the process gas, and at the same time absorb the entrainment in the crude synthesis gas after gasification The ash and arsenic and other poisons play a certain protective role. The sulfur-tolerant shift catalyst used in this process is usually also called sulfur-tolerant pre-shift catalyst. Compared with the main shift catalyst, the amount of this type of catalyst is much less, so that under the same load conditions, the gas space velocity of the catalyst bed in the pre-shift furnace is uniform. It is much higher than that of the main converter catalyst, some ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/888B01J23/883B01J23/885B01J23/889B01J35/10C01B3/16
CPCY02P20/52
Inventor 白志敏齐焕东余汉涛赵庆鲁田兆明王昊姜建波薛红霞陈依屏李文柱
Owner CHINA PETROLEUM & CHEM CORP
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