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Preparation method of catalyst for oxidization of hydrogen chloride for chlorine production

A catalyst, oxidation technology, applied in the direction of metal/metal oxide/metal hydroxide catalyst, preparation with chloride, physical/chemical process catalyst, etc., can solve the conditions that fail to reach large-scale industrialization, sodium hydroxide Overcapacity, unfavorable large-scale industrial promotion, etc., to achieve the effect of good reaction effect, low price, improved activity and stability

Active Publication Date: 2017-06-20
XIAN MODERN CHEM RES INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Almost all chlorine gas in industry is produced by electrolysis of sodium chloride aqueous solution. This method has two big problems: first, its power consumption reaches 2760kWh / ton, and the power consumption of the entire chlor-alkali industry accounts for about 100% of the total industrial consumption in the country. About 5% of electricity; followed by the co-production of sodium hydroxide while producing chlorine gas. Due to the rapid development of the chlorine-consuming industry in recent years, a large amount of excess capacity of sodium hydroxide has been caused
This preparation method improves the catalyst preparation process of Tsinghua University, but it is still only applicable to fluidized beds, which is not conducive to large-scale industrial promotion
[0012] Although the catalytic oxidation process of hydrogen chloride in the fluidized bed reaction system has been studied in detail internationally for many years, the conditions for large-scale industrialization have still not been achieved.

Method used

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  • Preparation method of catalyst for oxidization of hydrogen chloride for chlorine production
  • Preparation method of catalyst for oxidization of hydrogen chloride for chlorine production
  • Preparation method of catalyst for oxidization of hydrogen chloride for chlorine production

Examples

Experimental program
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Effect test

Embodiment 1

[0045] A certain amount of catalyzer is loaded into the fixed-bed tubular reactor, and the oxidation of hydrogen chloride to chlorine catalyst precursor is implemented according to the following weight percentages:

[0046]

[0047] Component A is copper oxide, component B is chromium oxide, component C is potassium chloride, and component D is silicon oxide. The obtained hydrogen chloride oxidation to chlorine catalyst is marked as A.

[0048] The catalyst for producing chlorine by oxidation of hydrogen chloride of the present invention is prepared by the following method.

[0049] a) Component A copper oxide is uniformly mixed with component B chromium oxide, put into a mortar and grind for 15 minutes, and dry;

[0050] b) Add the metal oxide powder obtained in step a) to an aqueous solution containing component C potassium chloride (1mol / L), the mass ratio of the metal oxide powder to the aqueous solution is 1:5, heat to reflux, and stir for 2 hours , filtered, washed,...

Embodiment 2

[0055] The hydrogen chloride oxidation of the present invention produces chlorine catalyst precursor according to following weight percent implementation:

[0056]

[0057] Component A is copper oxide, component B is chromium oxide, component C is potassium chloride, and component D is silicon oxide. The resulting hydrogen chloride oxidation to chlorine catalyst is marked as B.

[0058] The catalyst for producing chlorine by oxidation of hydrogen chloride of the present invention is prepared by the following method.

[0059] a) Component A copper oxide is uniformly mixed with component B chromium oxide, put into a mortar and grind for 15 minutes, and dry;

[0060] b) Add the metal oxide powder obtained in step a) into an aqueous solution containing component C potassium chloride (0.5mol / L), the mass ratio of the metal oxide powder to the aqueous solution is 1:5, heat to reflux, and stir to react 2h, filter, wash, dry, and roast at 350°C for 6h;

[0061] c) adding the mat...

Embodiment 3

[0070] The hydrogen chloride oxidation of the present invention produces chlorine catalyst precursor according to following weight percent implementation:

[0071]

[0072] Component A is copper oxide, component B is chromium oxide, component C is potassium chloride, and component D is silicon oxide. The resulting hydrogen chloride oxidation to chlorine catalyst is marked as D.

[0073] The preparation steps of the catalyst for hydrogen chloride oxidation to chlorine in the present invention are the same as in Example 1, the difference is the content of each component.

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Abstract

The invention discloses a preparation method of a catalyst for oxidization of hydrogen chloride for chlorine production. A catalyst precursor is prepared from the following components in percentage by mass: 50 to 60 percent of a component A, 35 to 50 percent of a component B, 1 to 2 percent of a component C and 3 to 5 percent of a component D, wherein the component A is chromic oxide; the component B is copper oxide; the component C is one or more of K<+>, Na<+> and Cs<+>; the component D is silicon oxide. The preparation method is characterized by comprising the following hydrogen chloride oxidization catalyst preparation steps: firstly, grinding the component A and the component B to obtain mixed metal oxide powder; secondly, immersing and modifying the metal oxide powder through the component C; finally, adding the component D, granulating and pressing the components, roasting, and carrying out fluorinated pore-forming activation through HF, thus obtaining the efficient hydrogen chloride oxidization catalyst.

Description

technical field [0001] The invention belongs to the field of catalysts, and in particular relates to a preparation method of a catalyst used to oxidize hydrogen chloride to produce chlorine. Background technique [0002] Chlorine is an important basic chemical raw material, widely used in polyurethane, silicone, chlorinated hydrocarbons, epoxy resin, chlorinated rubber, chlorinated high polymer and other new material industries, and in new energy industries such as polysilicon manufacturing. Used in household fine chemical industries such as disinfectants, detergents, food additives, cosmetic additives, etc., used in the synthesis of glycerin, chlorobenzene series, chloroacetic acid, benzyl chloride, PCl 3 Pesticide / pharmaceutical industries, as well as paper, textile, metallurgy and petrochemical industries. [0003] Almost all chlorine gas in industry is produced by electrolysis of sodium chloride aqueous solution. This method has two big problems: firstly, its power cons...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/86C01B7/04
Inventor 惠丰袁俊杨建明吕剑赵锋伟李亚妮张前李江伟余秦伟王为强梅苏宁
Owner XIAN MODERN CHEM RES INST
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