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Method and equipment for continuous preparation of metallic oxide material and catalyst

A metal material, oxide technology, applied in metal/metal oxide/metal hydroxide catalyst, oxide/hydroxide preparation, chemical instruments and methods, etc. Uniform dispersion, inability to obtain expected performance products, etc., to avoid precipitants and save industrial raw materials

Active Publication Date: 2010-06-23
SYNFUELS CHINA TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Usually the hydrothermal method is carried out in a closed pressure vessel, which requires strict control of operating conditions, otherwise the product with the expected performance cannot be obtained
[0014] However, it is generally difficult to obtain metal oxide materials with uniform particles by thermal hydrolysis of metal inorganic salt or organic metal salt solution, and it is difficult to evenly disperse additives.
[0015] The invention discloses a green method for preparing metal oxide hydrates, metal oxide materials and catalysts. The normal pressure precipitation (co-precipitation) method and the hydrothermal reaction method are organically integrated, which overcomes the harsh conditions and the need for conventional hydrothermal reaction methods. The shortcomings of being carried out in a closed container also overcome the problems of introducing one or more chemical reagents in the normal pressure co-precipitation method, which will cause a large amount of water consumption and generate a large amount of waste water and waste gas. The whole process is completely continuous, cyclic and zero. emission

Method used

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  • Method and equipment for continuous preparation of metallic oxide material and catalyst
  • Method and equipment for continuous preparation of metallic oxide material and catalyst
  • Method and equipment for continuous preparation of metallic oxide material and catalyst

Examples

Experimental program
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Effect test

Embodiment 1

[0139] In metal salt solution preparation reactor, Fe powder and Mn powder are according to the ratio of Fe: Mn=100: 18 (wt), are dissolved with the nitric acid of 35wt% from absorption tower, make the metal nitric acid that concentration is 25.5wt% Salt solution, adding an appropriate amount of aluminum sol;

[0140] Then, carry out thermal decomposition reaction with pressurized superheated steam (the temperature of described pressurized superheated steam is 140 ℃; pressure is 4.6bar) in metal salt solution decomposition reactor, reaction temperature 120 ℃, pressure 6bar, Made into brown-black precipitated slurry;

[0141] COLLECTION OF NO GENERATED 2 The gas is recovered by the compression system, and passed into the acid gas absorption tower, and the filtrate produced by slurry filtration is used as the absorption liquid for spray absorption, and the nitric acid with a concentration of 35wt% is produced, which is recycled as the solvent raw material for the configuration ...

Embodiment 2

[0144] In the transition metal salt solution preparation reaction kettle, block Fe, Cu and Zn are dissolved with 48wt% nitric acid from the absorption tower according to the ratio of Fe: Cu: Zn = 100: 6: 8 (wt), to prepare Concentration is the metal nitrate solution of 37.7wt%;

[0145] Carry out thermal decomposition reaction with pressurized superheated steam (the temperature of described pressurized superheated steam is 230 ℃; pressure is 28bar) in metal salt solution decomposition reactor, reaction temperature 190 ℃, pressure 15bar, make brown Red precipitated slurry, the slurry is filtered to make a filter cake with a solid content rate of 27.3wt%;

[0146] collected NO 2 The gas is recovered through a compression system (at a pressure of 3 bar), and passed into an acid gas absorption tower to use the filtrate produced by slurry filtration as an absorption liquid for spray absorption to produce nitric acid with a concentration of 48 wt%, which is recycled as a metal salt...

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PUM

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Abstract

The invention discloses a method and equipment for continuous preparation of metallic oxide and catalyst, and the preparation method comprises the following steps: dissolving metallic materials by salpeter solution to prepare metallic nitrate solution; introducing pressurization superheated vapor in metal salt solution to enable the metal salt solution to be hydrolyzed to obtain metallic oxide hydrate slurry and release NOx gas, and preparing the generated NOx gas into nitric acid for reuse; and filtering and drying the slurry to obtain the metallic oxide. The invention also discloses a method for preparing the catalyst by using the obtained metallic oxide and equipment for preparing the equipment, and the equipment comprises a metal salt preparation system, a metal salt solution hydrolysis reaction system, a product preparation system and a nitric acid preparation and recycling system. The method in the invention has the advantages of realizing continuity of the whole progress, lowering the production cost and realizing closed circulation and zero emission of the production progress.

Description

technical field [0001] The present invention relates to the technical field of catalysts and materials, more specifically, the present invention relates to methods and equipment for preparing metal oxide materials, including metal oxide hydrates and / or metal oxides and catalysts, and the methods and process equipment of the present invention are particularly It is suitable for the preparation of catalysts including Fischer-Tropsch synthesis of syngas to produce hydrocarbons and other metal oxide materials. The production method is an environment-friendly green chemical method. Background technique [0002] Metal oxides (including transition metal oxides), as the main active phase of most catalytic reactions, can usually provide the high specific surface area required for catalytic reactions, and the d and f electron bonding levels of transition metals are particularly suitable for The reactant molecules undergo chemical adsorption and activation; in addition, metal oxides a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B13/14B01J37/08B01J23/70C01G49/02
CPCC01G49/0072B01J35/1038B01J23/16B01J23/80B01J35/1014C01B21/42B01J23/70C01P2006/14C01B13/366B01J23/8892B01J23/78C01P2006/12C01P2006/11B01J37/033B01J35/0026C01G49/0018B01J23/72B01J37/0045B01J35/1019B01J23/10B01J37/10B01J35/31B01J35/613B01J35/633B01J35/615
Inventor 杨勇吴宝山许健相宏伟李永旺
Owner SYNFUELS CHINA TECH CO LTD
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