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Chromium-free and environment-friendly catalyst for synthesis of 1,1,1,3,3,3-hexafluoro-2-butene by gas-phase fluorination

A chemical synthesis and catalyst technology, which is applied in physical/chemical process catalysts, catalyst activation/preparation, organic chemistry, etc., can solve problems such as low catalyst activity, human health threats, ecological environment pollution, etc., and achieve large specific surface area and anti-sintering Superior performance, good anti-sintering ability at high temperature

Active Publication Date: 2021-11-23
XIAN MODERN CHEM RES INST
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The gas-phase fluorination reaction catalyst reported above uses chromium as the core component. However, as a heavy metal element, chromium, a large amount of discharge will cause serious pollution to the ecological environment; especially hexavalent chromium is a highly toxic substance that is harmful to animals and human health. pose a great threat
However, Fe-based gas-phase fluorination catalysts are prepared by traditional impregnation, co-precipitation and blending methods. Large particle size, poor thermal stability, and small specific surface area lead to low catalyst activity and poor selectivity.

Method used

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  • Chromium-free and environment-friendly catalyst for synthesis of 1,1,1,3,3,3-hexafluoro-2-butene by gas-phase fluorination
  • Chromium-free and environment-friendly catalyst for synthesis of 1,1,1,3,3,3-hexafluoro-2-butene by gas-phase fluorination
  • Chromium-free and environment-friendly catalyst for synthesis of 1,1,1,3,3,3-hexafluoro-2-butene by gas-phase fluorination

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] Embodiment 1: prepare M / MgF 2 catalyst

[0028] Dissolve 1.0M magnesium source and 0.01-0.1M modified metal ions in 50mL polyol solvent, add the fluorinating reagent dropwise to the above solution under stirring at 150-240°C, the dropping time is 15min, after the dropping is completed Stir again for 6-12h to obtain M / MgF 2 Dry gel; then roast in an air atmosphere or a hydrogen atmosphere at 300-500°C for more than 5 hours, and finally perform a fluorination treatment on the roasted material at a temperature of 150-400°C to obtain a catalyst. The fluorine reagents are gaseous hydrogen fluoride and dichlorodifluoromethane , one chlorodifluoromethane, one chlorotrifluoromethane any one. The textural properties of magnesium fluoride prepared under different magnesium sources, polyol solvents, coagulants, fluorinating reagents, and calcination temperatures are shown in Table 1.

[0029] The physicochemical property result of the magnesium fluoride-based catalyst of table ...

Embodiment 2

[0033] Adopt the same method to prepare M / MgF in embodiment 1 2 catalyst, which was applied to the gas-phase fluorination of CF 3 CHClCH 2 CCl 3 In the reaction of synthesizing HFO-1336, after running for 12 hours, the reaction results are as follows:

[0034] The reaction evaluation result of the magnesium fluoride-based catalyst of table 2 embodiment 2

[0035]

Embodiment 3

[0037] Adopt same method to prepare M / MgF in embodiment 1 2 catalyst, which was applied to the gas-phase fluorination of CF 3 CHClCH 2 CCl 3 In the reaction of synthesizing HFO-1336, after running for 12 hours, the reaction results are as follows:

[0038] The reaction evaluation result of the magnesium fluoride-based catalyst of table 3 embodiment 3

[0039]

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Abstract

The invention discloses a gas-phase catalytic CF 3 CHClCH 2 CCl 3 The invention discloses a chromium-free environment-friendly catalyst for synthesizing 1,1,1,3,3,3-hexafluoro-2-butene with anhydrous hydrogen fluoride and a preparation method thereof. It is to solve the environmental problems of traditional chromium-based fluorination catalysts. Extensive use of heavy metal chromium will cause a series of serious pollution and health problems, as well as the poor performance of traditional iron-based catalysts. The catalyst disclosed by the present invention consists of M / MgF 2 , where the matrix MgF 2 It has a rutile phase and a nano-spherical structure with a specific surface area greater than 120m 2 / g, high stability MgF with excellent sintering resistance at 500°C 2 , the active component M is selected from Co 3+ 、Ni 2+ , Fe 3+ , Zn 2+ , La 3+ 、Al 3+ , Ga 3+ , Mn 4+ 、Cu 2+ one or more of them. The preparation of the catalyst comprises the following steps: (1) preparing a polyol solution containing a magnesium source and doped with metal ions, adding a fluorination reagent dropwise at 150-240°C to obtain a catalyst xerogel; (2) drying the xerogel at 300-240°C Calcined at 500°C, and finally fluorinated at 150-400°C to obtain a chromium-free high-performance catalyst.

Description

technical field [0001] The invention relates to a catalyst, in particular to a gas phase catalytic CF 3 CHClCH 2 CCl 3 A chromium-free and environmentally friendly catalyst for the synthesis of 1,1,1,3,3,3-hexafluoro-2-butene by reacting with hydrogen fluoride. Background technique [0002] 1,1,1,3,3,3-hexafluoro-2-butene, referred to as HFO-1336, does not contain chlorine atoms in the molecule, and its ozone depletion potential (ODP) is zero. After entering the atmosphere, it can quickly react with OH free radicals and degrade, the atmospheric life is short (≤20d), and the GWP value is only 9, so it has little impact on the environment when used. In addition, the physical and chemical properties of HFO-1336 are equivalent to those of the existing fluorine-containing blowing agents HCFC-141b and HFC-245fa, and it has excellent foaming and heat insulation properties. economic benefits. [0003] So far, among the many known synthetic routes, CF 3 CHClCH 2 CCl 3 Synthes...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/138B01J27/12B01J35/08B01J37/03B01J37/26C07C21/18C07C17/20C07C17/23
CPCC07C17/206C07C17/208C07C17/23B01J27/12B01J27/138B01J37/036B01J37/26B01J35/23B01J35/51C07C21/18
Inventor 毛伟吕剑白彦波贾兆华韩升秦越王博赵波李晨曾纪珺
Owner XIAN MODERN CHEM RES INST
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