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Catalyst for preparing tetrafluoroethylene and hexafluoropropylene by catalytic cracking of trifluoromethane and preparation method thereof

A trifluoromethane, catalytic cracking technology, applied in the direction of chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of low catalyst conversion rate and low temperature reaction effect It can improve the service life and application performance, improve the low-temperature reaction activity, and improve the anti-carbon deposition ability.

Active Publication Date: 2022-05-24
SHANDONG DONGYUE CHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] The process of preparing tetrafluoroethylene / hexafluoropropylene by pyrolysis of trifluoromethane is simple in process, high in added value of the product, and has great industrialization prospects. However, in the case of no catalyst, the cracking of empty tubes alone, the reaction temperature is 1000°C, and the conversion rate is 10%- About 20%; the conversion rate is low, and there are many by-products, and the separation is difficult
The catalyst of this invention can effectively reduce the reaction temperature of trifluoromethane catalytic cracking reaction, but the catalyst used is prone to coking and deactivation, the service life of the catalyst is short, the conversion rate of the catalyst is not high under low temperature conditions, and the low temperature reaction effect is not good

Method used

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  • Catalyst for preparing tetrafluoroethylene and hexafluoropropylene by catalytic cracking of trifluoromethane and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] A preparation method of a catalyst for preparing tetrafluoroethylene and hexafluoropropylene by catalytic cracking of trifluoromethane, comprising the steps of:

[0033] take Al 2 O 3 100g of the carrier was put into a drying box and dried at 100°C for 3h; 13.5g La (NO 3 ) 3 Dissolve in 100ml of pure water to prepare an impregnation solution; put the dried carrier into the impregnation solution, soak it for 20min, take it out, put it in a drying box and dry it at 100 ℃ for 3h to obtain the precursor; take it out, put it in a roasting furnace, It was calcined at 400 °C for 6 h in a nitrogen atmosphere. Take out the calcined precursor and put it in In the reaction tube, pass N 2 , N 2 The flow rate is 300ml / min, and it is dried at a temperature of 300°C for 24h. Then pass trifluoromethane gas at 300°C for fluorination at a flow rate of 6 L / min, and turn off nitrogen after 2 h; pass trifluoromethane alone at a flow rate of 6 L / min, fluorination at 350° C. for 60 h, a...

Embodiment 2

[0035] A preparation method of a catalyst for preparing tetrafluoroethylene and hexafluoropropylene by catalytic cracking of trifluoromethane, comprising the steps of:

[0036] take AlF 3 100g of the carrier was put into a drying box and dried at 100°C for 3h; 13.5g La (NO 3 ) 3 Dissolve in 100ml of pure water to prepare an impregnation solution; put the dried carrier into the impregnation solution, soak it for 20min, take it out, put it in a drying box and dry it at 100 ℃ for 3h to obtain the precursor; take it out, put it in a roasting furnace, It was calcined at 400 °C for 6 h in a nitrogen atmosphere. Take out the calcined precursor and put it in In the reaction tube, pass N 2 , N 2 The flow rate is 300ml / min, and it is dried at a temperature of 300°C for 24h. Then pass trifluoromethane gas at 300°C for fluorination at a flow rate of 6 L / min, and turn off nitrogen after 2 h; pass trifluoromethane alone at a flow rate of 6 L / min, fluorination at 350° C. for 60 h, and...

Embodiment 3

[0038] A preparation method of a catalyst for preparing tetrafluoroethylene and hexafluoropropylene by catalytic cracking of trifluoromethane, comprising the steps of:

[0039] take Al 2 O 3 100g of the carrier was put into a drying box and dried at 100°C for 3h; 13.5g of CsNO 3 Dissolve in 100ml of pure water to prepare an impregnation solution; put the dried carrier into the impregnation solution, soak it for 20min, take it out, put it in a drying box and dry it at 100 ℃ for 3h to obtain the precursor; take it out, put it in a roasting furnace, It was calcined at 400 °C for 6 h in a nitrogen atmosphere. Take out the calcined precursor and put it in In the reaction tube, pass N 2 , N 2 The flow rate is 300ml / min, and it is dried at a temperature of 300°C for 24h. Then pass trifluoromethane gas at 300°C for fluorination at a flow rate of 6 L / min, and turn off nitrogen after 2 h; pass trifluoromethane alone at a flow rate of 6 L / min, fluorination at 350° C. for 60 h, and...

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Abstract

The invention provides a catalyst for preparing tetrafluoroethylene and hexafluoropropylene by catalytic cracking of trifluoromethane and a preparation method thereof. chemically made; the carrier is Al 2 o 3 or AlF 3 ; The active components are Cs, La, Sm, Pd, Pt, K or Na chlorides and nitrates or a combination of two or more. The preparation method of the invention is simple, can catalytically crack trifluoromethane under relatively low temperature and mild conditions, has low equipment requirements, low energy consumption, and low cost; the prepared catalyst can effectively reduce the reaction of catalytic cracking of trifluoromethane The conversion rate of the raw material and the selectivity of the target product can be improved under relatively mild conditions, which can effectively solve the problem of catalyst coking and improve the service life of the catalyst.

Description

technical field [0001] The invention relates to a catalyst for preparing tetrafluoroethylene and hexafluoropropylene by catalytic cracking of trifluoromethane and a preparation method thereof, belonging to the field of fluorine chemical catalyst preparation. Background technique [0002] Trifluoromethane (CHF 3 , HFC-23) is a by-product produced during the catalytic reaction of chloroform and HF to prepare difluoromonochloromethane (HCFC-22), and its yield is about 1.5-3.5wt% of the content of HCFC-22; -22 itself is used as the main raw material for the manufacture of perfluoroolefins such as tetrafluoroethylene (TFE), so difluorochloromethane is excluded from the emission reduction items stipulated in the Kyoto Protocol; therefore trifluoromethane (CHF 3 ) emissions will continue for a long time, the annual CHF generated 3 as many as tens of thousands of tons. Trifluoromethane is a greenhouse gas (GWP value of about 14800, equivalent to CO 2 14,800 times) and has a long...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/04B01J23/10B01J23/42B01J23/44B01J27/12C07C17/269C07C21/185C07C21/18
CPCC07C17/269B01J23/002B01J23/04B01J23/10B01J23/42B01J23/44B01J27/12C07C21/185C07C21/18Y02P20/584
Inventor 丁晨王鑫都荣礼王伟徐强
Owner SHANDONG DONGYUE CHEM