Hydrodehalogenation catalyst and preparation method of chlorotrifluoroethylene and trifluoroethylene

A technology of hydrodehalogenation and trifluorotrichloroethane, which is applied in the direction of dehalogenation preparation, chemical instruments and methods, catalyst carriers, etc., can solve the problems of high consumption of zinc powder, difficulty in obtaining high-quality TrFE, and low specific surface area. question

Pending Publication Date: 2021-11-16
SHANGHAI HUAYI GRP CO +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the industry mainly uses zinc powder to reduce 1,1,2-trifluorotrichloroethane to produce CTFE. However, this route consumes a lot of zinc powder and has high environmental protection costs. A new process route is urgently needed to replace it.
[0004] The synthesis of trifluoroethylene (TrFE) mainly includes the hydrogenation of CTFE and the cracking of tetrafluoroethane (HFC-134a), but at present, due to the limited source of raw materials and immature catalytic technology, its large-scale industrial application is still restricted.
However, the study found that both types of catalysts have different degrees of deactivation problems.
[0007] Chinese patent CN1065261 discloses that the noble metal-supported activated carbon catalyst with copper as a cocatalyst can be used for the hydrodechlorination of 1,1,2-trifluorotrichloroethane to produce chlorotrifluoroethylene and trifluoroethylene, and the adjustment of the copper content can change the three The formation ratio of chlorofluoroethylene and trifluoroethylene, and different noble metals such as palladium and platinum also affect the ratio of the two. The selectivity of chlorotrifluoroethylene and trifluoroethylene is usually greater than 90%, but the life of the catalyst is not long , the inactivation phenomenon appeared after 300 hours of reaction
[0008] Chinese patent CN1460549 has reported that the catalyst with coconut shell carbon as the carrier and copper palladium as the main active component is used for CFC-113 hydrodechlorination to prepare CTFE, and it is found that some alkali metals and alkaline earth metals can significantly improve the efficiency of CTFE as modification aids. Selectivity (>85%), but the catalyst still has obvious deactivation phenomenon, and the service life is less than 1000 hours
However, from the perspective of the carrier preparation process, due to the generally low specific surface area of ​​metal fluorides such as aluminum fluoride and the limited loading and dispersion of active metals, it is difficult to use these metal fluorides alone as carriers to prepare catalysts. The method to prepare aluminum fluoride with high specific surface area still has a lot of alumina components, which is unfavorable for the hydrogenation catalyst and the long-term operation reaction under the atmosphere of hydrogen chloride or hydrogen fluoride. Compared with the catalyst directly supported by activated carbon, its long-term service life is also in doubt
[0012] Although the existing catalysts can achieve a higher conversion rate of CFC-113, the performance of the catalyst is mostly aimed at improving the selectivity of CTFE, and other products of hydrogenation are less concerned, and it is difficult to obtain high-quality TrFE, and according to the polymer Monomer requirements, but also to minimize unwanted impurities in fluoroolefins

Method used

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Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0053] 4. Preparation of Hydrodehalogenation Catalyst

[0054] The hydrodehalogenation catalyst of the present invention can be formed by placing the main catalyst and the co-catalyst (ie, catalyst active components) on the carrier using methods known in the art. The method for carrying the catalyst active component on the catalyst carrier is not particularly limited, and can be a conventional method known in the art, such as excessive impregnation and equal volume impregnation, one-step impregnation and multi-step impregnation, etc. The catalyst components are loaded on the carrier that has been formed, and then the carrier loaded with the main catalyst and the co-catalyst is dried, calcined and reduced to obtain the desired catalyst.

[0055] In the present invention, the drying, calcination and reduction are all conventional methods for preparing catalysts. In one example of the present invention, the drying temperature is 100-150°C, preferably 110-140°C, more preferably 1...

Embodiment 1

[0070] Catalyst preparation:

[0071] Weigh a certain amount of ferric fluoride and add it into water at 70°C to form a solution. According to the mass content of ferric fluoride in the carrier as 1%, use a coating machine to spray and impregnate the ferric fluoride solution on 10 grams of nitric acid-treated porous Coal-based carbon (cylindrical activated carbon, φ2mm, purchased from Sinopharm Chemical Reagent Co., Ltd.), then dried at 120°C for 4 hours, and the dried sample was treated at 350°C for 4 hours under a nitrogen atmosphere to obtain a composite of activated carbon-ferric fluoride Material carrier, the specific surface area of ​​the carrier is 960m2 by nitrogen adsorption and desorption test 2 / g, the average pore diameter is 3.5nm.

[0072] Add 0.083g of palladium chloride to 10mL of deionized water, add hydrochloric acid dropwise to form an acidic solution of palladium chloride (pH=2), then impregnate the above-mentioned carrier with an equal volume of the palla...

Embodiment 2

[0074] Catalyst preparation:

[0075] Weigh 0.58g calcium nitrate (4 crystalline water) and 0.13g chromium nitrate (9 crystalline water) and dissolve in 50mL deionized water to configure mixed solution 1; weigh 0.77g potassium hydroxide and 0.38g potassium fluoride to dissolve In 50mL deionized water, configured as mixed solution 2; 10g carbon aerogel (synthesis reference Pekala, R.W.and C.T.Alviso (1992). "CarbonAerogels and Xerogels." MRS Online Proceedings Library 270 (1): 3-14 .) Disperse in 50mL of deionized water and keep stirring, add solution 1 and solution 2 dropwise at the same time, and continue stirring for 2 hours after the dropwise addition is completed. Then adjust the pH value to 2 with hydrofluoric acid, heat to 80°C and continue stirring for 2 hours. Then the mixture was filtered and washed, and dried at 120° C. for 4 hours, and the dried solid sample was treated at 300° C. for 4 hours under a nitrogen atmosphere to obtain a composite carrier of calcium fluo...

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Abstract

The invention discloses a hydrodehalogenation catalyst and a preparation method of chlorotrifluoroethylene and trifluoroethylene. The catalyst carrier for the hydrodehalogenation catalyst comprises a porous carbon-metal halide compound formed by firing a porous carbon substrate and a metal halide modifier, and the amount of metal halide in the catalyst carrier accounts for 0.01-10% by weight.

Description

technical field [0001] The invention relates to a hydrodehalogenation catalyst and a method for simultaneously preparing chlorotrifluoroethylene and trifluoroethylene. In addition to improved product selectivity, the catalysts of the present invention also have improved service life, thereby reducing operating costs. [0002] technical background [0003] Fluorine-containing olefins such as chlorotrifluoroethylene (CTFE) and trifluoroethylene (TrFE) have high added value in the field of fluorine chemical industry. One of the important raw materials of fluorine fine chemicals. At present, the industry mainly adopts zinc powder to reduce 1,1,2-trifluorotrichloroethane to produce CTFE, but this route consumes a lot of zinc powder and has high environmental protection costs, so a new process route is urgently needed to replace it. [0004] The synthesis of trifluoroethylene (TrFE) mainly includes the hydrogenation of CTFE and the cracking of tetrafluoroethane (HFC-134a), but it...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/128B01J27/138B01J27/125B01J32/00B01J35/10C07C17/23C07C21/18
CPCB01J27/128B01J27/138B01J27/125B01J23/002B01J35/1023B01J35/1061C07C17/23B01J2523/00B01J2523/17B01J2523/27B01J2523/821B01J2523/15B01J2523/824B01J2523/3706B01J2523/847C07C21/18
Inventor 廖湘洲粟小理陆子薇胡总卢磊杜丽君赖春波陆艳萍郑渝佳
Owner SHANGHAI HUAYI GRP CO
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