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Decarbonylation chlorination catalyst as well as preparation method and application thereof

A decarbonylation and chlorination catalyst, a catalyst technology, applied in physical/chemical process catalysts, chemical instruments and methods, preparation of organic compounds, etc., can solve the difficulty of synthesizing and separating chlorinated aromatic compounds, and the product quality is difficult to guarantee , increase the difficulty of separation, etc., to achieve the effect of reducing temperature, good adaptability, and reducing the amount of precious metals

Active Publication Date: 2018-05-04
SHANGHAI RES INST OF CHEM IND +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] However, the synthesis and separation of chlorinated aromatic compounds are difficult
For example: although there are many synthetic methods for compounds containing m-dichlorobenzene structure, direct chlorination or short-process chlorination is the best choice from the perspective of economy and practicability, but direct chlorination or short-process chlorination is the best choice. When synthesizing such compounds by process chlorination, often because the position of the substituent is not the preferred position, a large amount of isomeric by-products are inevitably produced during the preparation process, which increases the difficulty of separation
Another example: when the key intermediate 3,5-dichlorobenzoyl chloride used in the preparation of various pesticides and medicines is synthesized, the method disclosed in the Chinese invention patent with the application publication number CN103508880A needs to use sulfur trioxide and phosgene Compounds are not only poor in environmental protection, but also difficult to guarantee product quality; other routes described in public literature involve diazotization, hypophosphorous acid deamination, thionyl chloride and other highly dangerous and polluting processes

Method used

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  • Decarbonylation chlorination catalyst as well as preparation method and application thereof
  • Decarbonylation chlorination catalyst as well as preparation method and application thereof
  • Decarbonylation chlorination catalyst as well as preparation method and application thereof

Examples

Experimental program
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Effect test

Embodiment 1

[0042] Preparation of catalyst: at room temperature, the specific surface area is 200m 2 / g of activated aluminum oxide 10g, added to 15mL containing 1.67g of palladium chloride and 0.50g of gallium trichloride prepared by hydrochloric acid acid (pH <1) In the aqueous solution, slowly heat to boiling and maintain for 2h, then cool to below 40°C, collect the solid by filtration, wash with deionized water until the mother liquor is neutral, and then dry in an oven at 80°C to obtain the catalyst precursor About 12g. Take 5g of the prepared catalyst precursor and put it into a fixed-bed reactor, first purge the adsorbed moisture with nitrogen to a temperature of 200°C, maintain it for 2h and then further increase the temperature to 450°C, maintain it for 3h, and then slowly decrease the temperature to 80°C. Into a hydrogen-nitrogen mixture with a volume content of 10% (the volume fraction of hydrogen is 10%), keep the reduction until anhydrous gas is generated, then heat up to 200°C...

Embodiment 2

[0048] Catalyst preparation: at room temperature, the specific surface area is 200m 2 / g of activated aluminum oxide 10g, added to 15mL containing 1.67g palladium chloride, chloroplatinic acid 0.20g and gallium trichloride 0.50g prepared by hydrochloric acid acid (pH <1) In the aqueous solution, slowly heat to boiling and maintain for 2h, then cool to below 40°C, collect the solid by filtration, wash with deionized water until the mother liquor is neutral, and then dry in an oven at 80°C to obtain the catalyst precursor About 12g. Take 5g of the prepared catalyst precursor and put it into a fixed-bed reactor, first purge the adsorbed moisture with nitrogen to a temperature of 200°C, maintain it for 2h and then further increase the temperature to 450°C, maintain it for 3h, and then slowly decrease the temperature to 80°C. Into a hydrogen-nitrogen mixture with a volume content of 10% (the volume fraction of hydrogen is 10%), keep the reduction until anhydrous gas is generated, the...

Embodiment 3

[0053] Catalyst preparation: at room temperature, take the specific surface as 50m 2 / g of magnesium fluoride 10g, added to 15mL containing 0.83g palladium chloride, 0.10g chloroplatinic acid and 0.20g titanium tetrachloride prepared by hydrochloric acid acid (pH <1) In the aqueous solution, slowly heat to boiling, and further evaporate the solvent to obtain about 11.2 g of solid. Take 5g of the prepared catalyst precursor and put it into a fixed-bed reactor, first purge the adsorbed moisture with nitrogen to a temperature of 200°C, maintain it for 2h and then further increase the temperature to 450°C, maintain it for 3h, and then slowly decrease the temperature to 80°C. Fill in the hydrogen-nitrogen mixture with a volume content of 10%, keep the reduction until anhydrous gas is generated, then heat up to 200°C to reduce for 5 hours, then cool to room temperature in a nitrogen atmosphere, and then transfer the catalyst to the reagent bottle under nitrogen protection and seal it ...

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Abstract

The invention relates to a decarbonylation chlorination catalyst as well as a preparation method and application thereof. The decarbonylation chlorination catalyst comprises a carrier as well as a precious metal component and a metal modifying component which are loaded on the carrier, wherein the carrier is a porous inert carrier, and the particle size of the precious metal component is less thanor equal to 10nm; during preparation, a co-precipitation method or impregnation method is adopted, the precious metal component and the metal modifying component are loaded on the carrier, so that the decarbonylation chlorination catalyst is obtained; and the decarbonylation chlorination catalyst can be used for catalyzing decarbonylation chlorination reaction of an aroyl chloride compound, and achlorinated aromatic compound is prepared. Compared with the prior art, the decarbonylation chlorination catalyst provided by the invention has the advantages that the carrier is loaded with the precious component and metal modifying component which are finely dispersed, and reduction is carried out, so that the decarbonylation chlorination catalyst is obtained, the decarbonylation process of thearoyl chloride compound can be effectively catalyzed, rearrangement chlorination is carried out, the catalyst has good adaptability on chlorine-containing rigorous reaction conditions, reaction can be effectively catalyzed with extremely low catalyst usage amount, and a target product is obtained; meanwhile, the usage amount of precious metal is low, and decarbonylation chlorination temperature is lowered, so that the decarbonylation chlorination catalyst provided by the invention has broad application prospect.

Description

Technical field [0001] The invention belongs to the technical field of preparation of chlorinated aromatic compounds, and relates to a decarbonylation chlorination catalyst and a preparation method and application thereof. Background technique [0002] Chlorinated aromatic compounds are an important class of organic intermediates, which are widely used in the fields of medicine, pesticides, and new materials. Among them, the role of chlorinated aromatic compounds with special substituent positions in related fields has become increasingly prominent and has gradually attracted more and more attention. [0003] However, the synthesis and separation of chlorinated aromatic compounds are quite difficult. For example: For compounds containing m-dichlorobenzene structure, although there are many synthetic methods, from the perspective of economy and practicality, direct chlorination or short-process chlorination is the best choice, but direct chlorination or short-circuit chlorination i...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/44B01J23/62B01J23/80B01J23/89B01J27/135B01J27/185B01J31/22B01J31/24B01J31/26C07C51/62C07C63/70
CPCC07C51/62B01J23/44B01J23/62B01J23/80B01J23/8906B01J27/135B01J27/1856B01J31/2273B01J31/2404B01J31/26B01J2531/824B01J35/394B01J35/393C07C63/70
Inventor 曹育才李永清高振华王凡沈安
Owner SHANGHAI RES INST OF CHEM IND