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Molybdenum based catalyst

A molybdenum-based catalyst and catalyst technology, applied in the direction of catalyst activation/preparation, physical/chemical process catalyst, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problem of slow metabolism and removal, and the use of chromium catalyst Problems such as low temperature and injury

Active Publication Date: 2020-07-10
泉州宇极新材料科技有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, with the deepening of research, people found that chromium catalyst still has the defects of low use temperature, low catalytic activity, short service life, and difficulty in recycling. More importantly, chromium is toxic and can cause great harm to people. Especially high-valent chromium has strong carcinogenicity
According to research, hexavalent chromium is 100 times more toxic than trivalent chromium, and is easily absorbed and accumulated in the body, and its metabolism and clearance are slow

Method used

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  • Molybdenum based catalyst
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  • Molybdenum based catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0084] According to the percentage composition of molybdenum ion and nickel element is 90% and 10%, molybdenum simple substance and nickel nitrate are uniformly mixed, pressed into tablets to form a catalyst precursor, and 10mL of the catalyst precursor is filled with an inner diameter of 1 / 2 inch and a length of 30cm The tubular reactor made of Monel material is fed with nitrogen and roasted at 450°C for 8 hours, and the nitrogen space velocity is 200h -1 , lower the temperature to 300°C, then seal the tubular reactor, vacuumize first, and then introduce fluorine gas. times, and less than or equal to 5 / 2 times, activated for 12 hours, and the residual fluorine gas was absorbed by dry soda lime to obtain a molybdenum-based catalyst.

Embodiment 2

[0086] The preparation process of the catalyst is basically the same as in Example 1, except that the percentage composition of molybdenum ions and nickel elements is 100% and 0%.

Embodiment 3

[0088] The preparation process of the catalyst is basically the same as in Example 1, except that the percentage composition of molybdenum ions and nickel elements is 80% and 20%.

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Abstract

The invention discloses a high-activity molybdenum-based catalyst and belongs to the field of chemical synthesis. The high-activity molybdenum-based catalyst is composed of, by mass, 60-100% of molybdenum ions and 0-40% of auxiliaries, the molybdenum ions are one or multiple of trivalent molybdenum ions, tetravalent molybdenum ions, pentavalent molybdenum ions and hexavalent molybdenum ions, and the auxiliaries are other metal elements. Total amount of fluorine or molybdenum hexafluoride fed at an activation stage is equal to a sum of theoretical amount of fluorine or molybdenum hexafluoride consumed by a precursor of the molybdenum ions and theoretical amount of fluorine or molybdenum hexafluoride consumed by metal element auxiliaries, and hexavalent molybdenum is prone to loss, so that molybdenum ion reduction is controlled in a trivalent, tetravalent or pentavalent state to the greatest extent when consumption of fluorine is calculated. The molybdenum-based catalyst is high in using temperature, high in catalytic activity and long in service life and is mainly used for vapor-phase catalysis of halogenated olefin at high temperature for fluorine-chlorine exchange reaction to prepare fluorine-containing olefin.

Description

technical field [0001] The invention relates to a molybdenum-based catalyst, in particular to gas-phase catalyzed fluorine-chlorine exchange reaction of halogenated olefins at high temperature to prepare fluorine-containing olefins. Background technique [0002] In order to fulfill the Montreal Protocol aimed at protecting the Earth's ozone layer, countries around the world have launched hydrofluorocarbons (HFCs) and hydrofluoroolefins (HFOs) with zero ODP values, thereby phasing out chlorofluorocarbons (CFCs) and hydrofluorocarbons (CFCs) with non-zero ODP values Chlorocarbons (HCFCs). At present, HFCs and HFOs have been widely used as refrigerants, cleaning agents, foaming agents, fire extinguishing agents, etching agents, etc. [0003] At present, the industrial production of HFCs or HFOs mostly adopts the method of gas-phase catalytic fluorine-chlorine exchange reaction of halogenated organic substances. This method has the advantages of simple process, easy continuous ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/28B01J23/882B01J23/883B01J23/34B01J23/881B01J23/885B01J23/652B01J23/68B01J37/08B01J37/26C07C17/20C07C21/18
CPCB01J23/002B01J23/28B01J23/34B01J23/6525B01J23/686B01J23/881B01J23/882B01J23/883B01J23/885B01J37/088B01J37/26C07C17/206C07C21/18
Inventor 权恒道张呈平张小玲庆飞要
Owner 泉州宇极新材料科技有限公司