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Superfine powder composite metallic oxide catalyst and application thereof

A composite metal and ultrafine powder technology, applied in the direction of metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, chemical/physical process, etc., can solve the problem of low metal content, high cost and large usage and other problems, to achieve the effect of high conversion rate of residual oil, high yield of distillate oil and high economic applicability

Active Publication Date: 2013-01-09
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantages of this type of catalyst are: the catalyst aqueous solution has poor compatibility with heavy oil, and the dispersion effect is not good
But the shortcoming of above-mentioned catalyst is: organometallic compound molecular weight is big, and metal content is low, and the usage amount when measuring with metal content is large, and cost is expensive

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Prepare catalyst A according to the sol-gel method: take by weighing the ammonium molybdate and ferric nitrate of calculated amount according to the amount of producing 15g catalyst, add deionized water respectively for dissolving, stir the ammonium molybdate solution at room temperature and add ferric nitrate solution dropwise to form Yellow precipitate. Add citric acid in an amount of 0.5 moles of molybdenum. Stir well to form a clear light yellow solution, and then use ammonia water to adjust the pH value to 3.0-13.0. Dry at 105°C overnight to obtain a gel, and finally bake at 500°C for 4 hours to obtain catalyst A, which is a composite Mo-Fe oxide ultrafine powder. The molar ratio of Mo and Fe is 3:2, and the average particle size of catalyst A is 20-100nm.

Embodiment 2

[0026] Prepare catalyst B according to the sol-gel method: weigh the calculated amount of ammonium molybdate, iron nitrate and cobalt nitrate according to the amount of 15g catalyst produced, add deionized water to dissolve, mix iron nitrate and cobalt nitrate aqueous solution, and stir at room temperature Ammonium molybdate solution and a mixed solution of ferric nitrate and cobalt nitrate were added dropwise to form a yellow-red precipitate. Add citric acid in an amount of 0.5 moles of molybdenum. Stir well to form a clear yellow-red solution, then adjust the pH value to 3.0-13.0 with ammonia water. Dry at 105°C overnight to obtain a gel, and finally bake at 500°C for 4 hours to obtain catalyst B, which is a composite Mo-Fe-Co oxide superfine Powder, wherein the molar ratio of Mo, Fe and Co is 2:2:1, and the average particle size of catalyst B is 20-100nm.

Embodiment 3

[0028] Prepare catalyst C according to the coprecipitation method: weigh the calculated amount of ammonium molybdate and ferric nitrate according to the amount of 15g catalyst produced, add deionized water to dissolve them respectively, stir the ammonium molybdate solution at room temperature and add ferric nitrate solution dropwise to form a yellow precipitate . Then adjust the pH value with ammonia water to make the precipitation more complete. Dry at 105°C overnight, and finally bake at 500°C for 4 hours to obtain catalyst C, which is a composite Mo-Fe oxide ultrafine powder, wherein the molar ratio of Mo to Fe is 3:1, and the average particle size of catalyst C is 20- 100nm.

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PUM

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Abstract

The invention relates to superfine powder composite metallic oxide catalyst and application thereof. The catalyst is a composite metallic oxide containing metal Mo and metal Fe, wherein the molar ratio of the Mo to the Fe is (1-6):(1-10), and the average particle diameter of the catalyst is 20-100nm. The catalyst of the invention is a nano-scale solid powder catalyst which has strong hydrogenation performance and good dispersibility, can be better suitable for the hydrogenation process of a heavy oil suspension bed and can be used for machining poor-quality heavy oil containing high impurity content of metals, sulfur, nitrogen, asphaltene and the like. The obtained residual oil has high conversion ratio, and the obtained distillate oil has high yield. Because the consumption of the catalyst is low, the invention has higher economic applicability.

Description

technical field [0001] The present invention relates to an ultrafine powder composite metal oxide catalyst and its application, more specifically, it is an ultrafine powder catalyst containing a composite metal oxide of Fe metal and Mo metal, which is used in heavy oil refueling in a suspended bed in the hydrogen process. Background technique [0002] With the increasingly heavy and inferior crude oil and the increasing demand for light oil products, the efficient utilization technology of heavy oil and residual oil has attracted the attention of researchers. The hydrogenation process of residual oil is one of the important research directions, which can obtain as many liquid products as possible and remove impurities such as metals and asphaltenes. Existing reactor forms include fixed bed, moving bed, ebullating bed and suspension bed. Among them, the suspension bed hydrogenation has good adaptability to low-quality residual oil with high impurities such as metals, sulfur...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/881
Inventor 郜亮刘元东温朗友宗保宁慕旭宏俞芳管炳伟时昭
Owner CHINA PETROLEUM & CHEM CORP