CN110743618B - Aluminum-magnesium-boron powder/graphite alkyne mixed carrier loaded metal catalyst and preparation and application thereof - Google Patents

Aluminum-magnesium-boron powder/graphite alkyne mixed carrier loaded metal catalyst and preparation and application thereof Download PDF

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CN110743618B
CN110743618B CN201910941382.0A CN201910941382A CN110743618B CN 110743618 B CN110743618 B CN 110743618B CN 201910941382 A CN201910941382 A CN 201910941382A CN 110743618 B CN110743618 B CN 110743618B
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赵佳
王柏林
岳玉学
李小年
王赛赛
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Zhejiang University of Technology ZJUT
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Abstract

The invention has provided a aluminium-magnesium-boron powder/graphite alkyne mixed carrier to load the metal catalyst and its preparation method and application, the graphite alkyne carrier of the catalyst of the invention and mixed carrier formed by aluminium-magnesium-boron powder have better dispersion effect of metal, the catalytic activity is higher, the stability is better, the metal is through the form of coordinating with ionic liquid, stabilize in the external surface layer of the catalyst, has reduced the influence of mass transfer, has improved the dispersity of the metal at the same time, introduce the external static electric field into the preparation of metal-based catalyst loading ionic liquid for the first time, has promoted the enrichment of the metal active center in the ionic liquid surface layer, because the metal active center of the catalyst of the invention distributes in the ionic liquid surface layer, has reduced the influence of the substrate diffusion, under the reaction condition evaluated, the induction period of the catalyst disappears; the invention fundamentally solves the defects of low gas metal dispersibility and low mass transfer in the supported ionic liquid catalyst system.

Description

Aluminum-magnesium-boron powder/graphite alkyne mixed carrier loaded metal catalyst and preparation and application thereof
(I) technical field
The invention relates to an aluminum-magnesium-boron powder/graphite alkyne mixed carrier loaded metal catalyst, and preparation and application thereof.
(II) background of the invention
Chloroethylene is a monomer of polyvinyl chloride (PVC) which is one of five synthetic resins in the world, and is mainly produced by a calcium carbide acetylene method and a petroleum ethylene method. The existence of energy sources rich in coal, lean oil and little gas in China determines that the calcium carbide acetylene method will continue to be the main process for producing vinyl chloride in China in a long time in the future, namely mercury chloride catalyzes the reaction of acetylene and hydrogen chloride to generate vinyl chloride. However, highly toxic mercuric chloride catalysts severely pollute the environment and harm human health. Therefore, the development of the non-mercury catalyst is necessary for the sustainable development of the industry for synthesizing vinyl chloride by the acetylene method of calcium carbide.
Gold, ruthenium, rhodium, copper catalysts are considered as potential substitutes for non-mercury catalysts in the industry of preparing vinyl chloride by the calcium carbide process. The metal-based catalyst loaded with the ionic liquid is widely applied to the process of preparing vinyl chloride by an acetylene hydrochlorination method. For example, Chinese patent CN104703953A discloses a method for loading ionic liquid and metal on solid and applying the ionic liquid and metal to acetylene hydrochlorination reaction, and the selected solid carrier has a specific surface area of more than 0.1m2The solid has a pore volume of more than 0.02mL/g, the cation of the selected ionic liquid is an imidazolium cation, a pyridinium cation or a pyrrolidinium cation, the anion can be any anion, and the selected metal is mainly noble metal represented by Au and Pd. In this patent application, the metal is dispersed in the ionic liquid layer, and although the catalytic activity is high, the evaluation results show that the acetylene conversion rate after 500 hours of reaction is only about 60%. Chinese patent CN104936933A discloses a method for preparing a catalyst. In this patent application, the metal is first anchored to the carbon support surface and then the metal surface is covered with a layer of ionic liquid. However, the catalyst has short catalytic life and no industrial application example.
In summary, the metal agglomeration caused by the metal dispersed in the ionic liquid layer (fig. 1a) and the metal dispersion and mass transfer caused by the metal anchored on the surface of the carbon carrier and the ionic liquid layer (fig. 1b) loaded in the ionic liquid-loaded metal-based catalyst system may be important reasons for the poor catalytic life of the two ionic liquid-loaded metal-based catalyst systems. Chinese patent CN104936933A emphasizes that the metal is dispersed in the ionic liquid layer (fig. 1a) or the surface of the support (fig. 1b) mainly because both the ionic liquid layer and the metal are physically bound to the support without any chemical linkage.
In the present patent application, a new preparation strategy of supported ionic liquid catalyst systems is proposed. The metal active center is enriched to the outer surface of the catalyst, namely the ionic liquid outer surface layer (figure 2), in a chemical bond mode under the action of an external static electric field, so that the influence of substrate transmission on the catalytic performance is remarkably reduced, and meanwhile, the dispersion degree of metal in the ionic liquid layer is improved in a mode of chemical coordination of the metal active center and the ionic liquid of the surface layer. The method has potential application value in the process of producing vinyl chloride by the calcium carbide method.
Disclosure of the invention
The invention aims to provide an aluminum-magnesium-boron powder/graphite alkyne mixed carrier supported metal catalyst and preparation and application thereof, and the invention fundamentally solves the defects of low gas metal dispersibility and low mass transfer in a supported ionic liquid catalyst system.
The technical scheme of the invention is as follows:
an aluminum-magnesium-boron powder/graphite alkyne mixed carrier supported metal catalyst is prepared by the following method:
(1) mechanically mixing a graphite alkyne carrier with aluminum-magnesium-boron powder for 2-5 hours, and then roasting for 2-8 hours at 200-800 ℃ in an inert gas atmosphere to obtain a mixed carrier;
the graphite alkyne carrier can be pure graphite alkyne powder, graphite alkyne films, graphite alkyne particles and other graphite alkyne with any morphology, or graphite alkyne powder, graphite alkyne films, graphite alkyne particles and other graphite alkyne particles growing on a metal (such as copper) substrate;
the mass ratio of the graphite alkyne carrier to the aluminum-magnesium-boron powder is 1: 0.1 to 10;
the inert gas is one or a mixture of more than two of nitrogen, argon and helium in any proportion;
the mechanical mixing can be carried out by stirring and mixing with a mechanical stirring paddle;
(2) dissolving ionic liquid in a solvent, uniformly stirring, adding the mixed carrier obtained in the step (1), soaking for 2-10h, and drying (180 ℃) to obtain a solid product loaded with the ionic liquid;
the mass ratio of the ionic liquid to the mixed carrier is 1-20: 100, under this step of operation, the ionic liquid can be considered as being fully loaded;
the solvent is one or a mixed solvent of more than two of toluene, nitrogen-nitrogen dimethylformamide, nitrogen alkyl pyrrolidone, thionyl chloride and acetone in any proportion.
The volume dosage of the solvent is 5-100 mL/g based on the mass of the ionic liquid;
the ionic liquid is selected from one or a mixture of more than two of the following formulas (I) to (V) in any proportion;
Figure BDA0002222982840000021
in the formula (I), the compound is shown in the specification,
R1is H, CH3Or C2H5；
R2Is CnH2n+1Sulfur, oxygen or nitrogen atoms, n is an integer and n is more than or equal to 1 and less than or equal to 14;
R3is CkH2k+1K is an integer and is not less than 1 and not more than 4;
X-is chloride ion, bromide ion, hexafluorophosphate radical, tetrafluorophosphate radical, bis (trifluoromethanesulfonyl) imide radical, tetrafluoroborate radical or imide radical;
Figure BDA0002222982840000022
in the formula (II), the compound is shown in the specification,
R1、R2、R3、R4each independently is CnH2n+1Sulfur, oxygen or nitrogen atoms, n is an integer and n is more than or equal to 1 and less than or equal to 6;
X-is chloride ion, bromide ion, hexafluorophosphate radical, tetrafluorophosphate radical, bis (trifluoromethanesulfonyl) imide radical, tetrafluoroborate radical or imide radical;
Figure BDA0002222982840000023
in the formula (III), the compound represented by the formula (III),
R1、R2、R3、R4each independently is CnH2n+1Sulfur, oxygen or nitrogen atoms, n is an integer and n is more than or equal to 1 and less than or equal to 6;
X-is chloride ion, bromide ion, hexafluorophosphate radical, tetrafluorophosphate radical, bis (trifluoromethanesulfonyl) imide radical, tetrafluoroborate radical or imide radical;
Figure BDA0002222982840000024
in the formula (IV), the compound is shown in the specification,
R1、R2each independently is CnH2n+1N is an integer and n is not less than 1 and not more than 6;
R3is CnH2n+1Sulfur, oxygen or nitrogen atoms, n is an integer and n is more than or equal to 1 and less than or equal to 6;
X-is chloride ion, bromide ion, hexafluorophosphate radical, tetrafluorophosphate radical, trifluoromethanesulfonimide radical, tetrafluoroborate radical or iminate radical;
Figure BDA0002222982840000031
in the formula (V), the compound represented by the formula (V),
R1、R2each independently is CnH2n+1N is an integer and n is not less than 1 and not more than 6;
R3is CnH2n+1Sulfur, oxygen or nitrogen atoms, n is an integer and n is more than or equal to 1 and less than or equal to 6;
X-is chloride ion, bromide ion, hexafluorophosphate radical, tetrafluorophosphate radical, bis (trifluoromethanesulfonyl) imide radical, tetrafluoroborate radical or imide radical;
preferably, the ionic liquid is selected from one of the following:
the mass ratio of the triphenylphosphine bistrifluoromethanesulfonimide salt to the triphenylphosphine ethyl bromide is 4: 1;
the mass ratio of the triphenylphosphine bistrifluoromethanesulfonimide salt to the N-amyl-ethylpiperidine chloride salt is 1: 1;
the mass ratio of the 1-propyl-2, 3-dimethyl imidazole bistrifluoromethane sulfimide salt to the 1-hexyl-2, 3-dimethyl imidazole bistrifluoromethane sulfimide salt is 1: 1;
the mass ratio of 1-butyl-3-methylimidazole hexafluorophosphate to 1-propyl-3-butylimidazole tetrafluoroborate is 1: 4;
the mass ratio of 1-butyl-3-methylimidazole hexafluorophosphate to azomethylpyrrolidone hydrochloride is 3: 7;
the mass ratio of 1-butyl-2, 3-dimethyl imidazole tetrafluorophosphate to triphenyl ethyl phosphine bromide is 1: 1;
(3) dissolving metal salt in a solvent, uniformly stirring, adding the ionic liquid loaded solid product obtained in the step (2), soaking in an external static electric field for 2-4 h, and then drying (180 ℃) for later use;
the mass ratio of metal elements contained in the metal salt to the mixed carrier is 0.05-20: 100, under the operation of the step, the metal elements can be regarded as full load;
the solvent used in the step is the same as the solvent in the step (2), and the volume consumption of the solvent in the step is 0.5-10 mL/g based on the mass of the metal salt;
the metal salt can be marked as MX, wherein M is a metal cation and is selected from one or more of gold, ruthenium, rhodium and copper, and X is a non-metal anion and is selected from one or more of nitrate radical, sulfate radical, chlorine, bromine, dicyandiamide radical, thiosulfate radical, sulfite radical, pyrrolidone radical, pyridine radical, ammonium radical, phosphate radical, pyrophosphate radical, triphenylphosphine, poly phthalocyanine radical, thiophenol, phthalocyanine, dichloro (1, 10-phenanthroline) radical and acetyl pyruvic acid;
the voltage of the external static electric field is 0.2-4 kV;
(4) dispersing the product obtained in the step (3) in a mixed solution of a solvent and dimethyldichlorosilane, then placing the mixed solution on a rotary mixer for 10-14 h at 40-60 ℃, then dipping the mixed solution in an external static electric field for 2-4 h, and drying the dipped product in a specific atmosphere (the drying temperature is 180 ℃) to obtain the aluminum-magnesium-boron powder/graphite alkyne mixed carrier loaded metal catalyst;
in the mixed solution of the solvent and the dimethyldichlorosilane, the used solvent is the same as the solvent in the step (2), and the ratio of the solvent to the dimethyldichlorosilane is 50-400: 1 (mL: g);
the volume usage of the mixed solution of the solvent and the dimethyldichlorosilane is 5-60 mL/g based on the mass of the product obtained in the step (3);
the specific atmosphere can be selected from one or a mixture of several of nitrogen, argon, air, oxygen, hydrogen, acetylene, hydrogen chloride, methane, oxygen and chlorine;
the voltage of the external static electric field is 0.2-4 kV.
The aluminum-magnesium-boron powder/graphite alkyne mixed carrier loaded metal catalyst prepared by the method can be applied to the reaction for synthesizing chloroethylene by a calcium carbide method.
Specifically, the application method comprises the following steps:
the prepared catalyst is filled in a fixed bed reactor, the reaction temperature is 100-200 ℃, the reaction pressure is 0.1-0.5 MPa, and raw material gases HCl and C are introduced2H2Then vinyl chloride can be obtained through reaction;
further, the raw material gases HCl and C2H2The ratio of the amounts of substances n (HCl)/n (C)2H2) 0.9-1.2/1; the volume space velocity of acetylene is 10-100 h-1。
The catalyst of the invention has high stability in the reaction of synthesizing chloroethylene, and does not show the phenomenon of catalyst deactivation after running for 2000 hours for a long time.
Compared with the prior art, the invention has the following advantages:
1. specificity of the vector. The preparation method provided by the invention has the advantages that the metal dispersion effect in the mixed carrier formed by the graphite alkyne carrier and the aluminum-magnesium-boron powder is better, the catalytic activity is higher, and the stability is better.
2. The metal active centers are present in different positions. In the publicly reported literature and patents, metals are dispersed in the center of the ionic liquid (fig. 1a) or anchored. The metal in the application is stabilized on the outer surface layer of the catalyst (figure 2) in a form of coordination with the ionic liquid, so that the influence of mass transfer is reduced, and meanwhile, the dispersion degree of the metal is improved.
3. The external static electric field is introduced into the preparation of the metal-based catalyst loaded with the ionic liquid for the first time, so that the enrichment of metal active centers on the surface layer of the ionic liquid is promoted.
4. The induction period was eliminated. Because the active center of the catalyst metal is distributed on the surface layer of the ionic liquid, the influence of substrate diffusion is reduced, and the induction period of the catalyst disappears under the evaluated reaction condition. The induction period of the catalyst in the publicly reported literature and patent is 2-10 h.
(IV) description of the drawings
FIG. 1: schematic diagram of the ionic liquid supported metal-based catalyst system in the published patent: a) the metal is dispersed in the middle of the ionic liquid layer; b) the metal is distributed on the surface of the catalyst carrier;
FIG. 2: the invention discloses a schematic diagram of a metal-based catalyst system for loading ionic liquid.
(V) detailed description of the preferred embodiments
The present invention will be described with reference to specific examples. It should be noted that the examples are only intended to illustrate the invention further, but should not be construed as limiting the scope of the invention, which is in no way limited thereto. Those skilled in the art may make insubstantial modifications and adaptations to the invention described above.
In the following examples, the graphdiyne is obtained from Jiangsu Xiancheng nanometer Material science and technology Limited and has a specific surface area of 500-1000 m2g-1；
The aluminum magnesium boron powder is purchased from Shanghai pure industry Co.
Example 1
Preparation of the catalyst:
1) selecting 9.1g of a graphite alkyne film carrier and 0.91g of aluminum-magnesium-boron powder, mechanically mixing for 3 hours, and then roasting for 2 hours at 200 ℃ in a nitrogen atmosphere to obtain a solid sample for later use.
2) Dissolving 0.08g of triphenylphosphine bis (trifluoromethanesulfonyl) imide salt and 0.02g of triphenylphosphine ethyl bromide in 5mL of toluene, stirring uniformly, adding the solid sample obtained in the step 1), soaking for 2h, and drying at 180 ℃ for later use. Wherein the mass loading of the ionic liquid is 1%.
3) Dissolving 0.009g chloroauric acid in 0.05mL toluene, stirring well, adding the sample obtained in step 2), immersing in an external 0.2kV static electric field for 2h, and drying at 180 ℃ for later use. Wherein the mass loading of the gold element is 0.05 percent.
4) 10.109g of the solid sample obtained above was redispersed in a mixed solution of 50mL of toluene and 1.0g of dimethyldichlorosilane. And the mixture obtained above was subjected to a spinning treatment for 10h at 40 ℃ on a spinner. And then soaking in an additional 4kV static electric field for 2h, and drying at 180 ℃ in a nitrogen atmosphere to obtain the required solid catalyst.
Evaluation of catalyst Performance:
1.5g of the catalyst is applied to acetylene hydrochlorination in a fixed bed reactor, and the reaction conditions are as follows: the temperature is 100 ℃, the pressure is 0.1MPa, and the mass ratio of the raw material gas substances n (HCl)/n (C)2H2) 0.9/1, acetylene volume space velocity of 100h-1Under the condition of (1), the induction period is 0h, and after the reaction is 2000h, the acetylene conversion rate is 94% and the vinyl chloride selectivity is 99.5%.
Example 2
Preparation of the catalyst:
1) selecting 2g of graphite alkyne powder and 8g of aluminum-magnesium-boron powder, mechanically mixing for 2h, and then roasting for 3h under the conditions of argon atmosphere and 300 ℃, so as to obtain a solid sample for later use.
2) Dissolving 0.25g of triphenylphosphine bis (trifluoromethanesulfonyl) imide salt and 0.25g of N-pentyl-ethylpiperidine chloride ionic liquid in 5mL of nitrogen-nitrogen dimethylformamide, stirring uniformly, adding the solid sample obtained in the step 1), soaking for 3h, and drying at 180 ℃ for later use. Wherein the mass loading of the ionic liquid is 5%.
3) Dissolving 0.103g of ruthenium chloride in 0.5mL of nitrogen-nitrogen dimethylformamide, stirring uniformly, adding the sample obtained in the step 2), and soaking in an external 3kV static electric field for 2 hours. After 5h, drying at 180 ℃ for later use. Wherein the mass loading of the ruthenium element is 0.5 percent.
4) 12.5g of the solid sample obtained above was redispersed in 600mL of a mixed solution of N-dimethylformamide and 6.0g of dimethyldichlorosilane. And the mixture obtained above was subjected to a spinning treatment at 45 ℃ for 11h on a spinner. And then dipping the catalyst in an externally added 0.2kV static electric field for 2.5h, and drying the catalyst at 180 ℃ in a hydrogen atmosphere to obtain the required solid catalyst.
Evaluation of catalyst Performance:
4.5g of the catalyst is applied to acetylene hydrochlorination in a fixed bed reactor, and the reaction conditions are as follows: the temperature is 110 ℃, the pressure is 0.2MPa, and the mass ratio of the raw material gas substances n (HCl)/n (C)2H2) 1.0/1, acetylene volume space velocity of 10h-1Under the condition of (1), the induction period is 0h, and after the reaction is 2000h, the acetylene conversion rate is 96 percent and the vinyl chloride selectivity is 97.5 percent.
Example 3
Preparation of the catalyst:
1) selecting 8g of graphite alkyne powder and 2g of aluminum-magnesium-boron powder, mechanically mixing for 4h, and then roasting for 8h under the conditions of nitrogen atmosphere and 400 ℃, so as to obtain a solid sample for later use.
2) 0.4g of 1-propyl-2, 3-dimethyl imidazole bistrifluoromethane sulfimide salt and 0.4g of 1-hexyl-2, 3-dimethyl imidazole bistrifluoromethane sulfimide salt ionic liquid are dissolved in 8mL of toluene, and after uniform stirring, the solid sample obtained in the step 1) is added, soaked for 4h and dried at 180 ℃ for later use. Wherein the mass loading of the ionic liquid is 8%.
3) 4.53g of copper phthalocyanine is dissolved in 9.1mL of toluene, the mixture is uniformly stirred and then added with the sample obtained in the step 2), the sample is immersed in an external 3kV static electric field for 3 hours, and the sample is dried at 180 ℃ for standby. Wherein the mass loading of the copper element is 5 percent.
4) 14.81g of the solid sample obtained above was redispersed in a mixed solution of 300mL of toluene and 5.0g of dimethyldichlorosilane. And the mixture obtained above was subjected to a spinning treatment for 12h at 50 ℃ on a spinner. And then dipping the catalyst in an externally added 2kV static electric field for 3h, and drying the catalyst at 180 ℃ in an acetylene atmosphere to obtain the required solid catalyst.
Evaluation of catalyst Performance:
the catalyst 3.0g is applied to acetylene hydrochlorination reaction in a fixed bed reactor, and the reaction conditions are as follows: temperature 120 ℃ and pressureForce 0.3MPa, ratio of the quantities of the feed gas substances n (HCl)/n (C)2H2) 1.1/1, acetylene volume space velocity of 20h-1Under the condition of (1), the induction period is 0h, and after the reaction is 2000h, the acetylene conversion rate is 98 percent and the chloroethylene selectivity is 98.5 percent.
Example 4
Preparation of the catalyst:
1) selecting 2.5g of a graphite alkyne film and 7.5g of aluminum-magnesium-boron powder, mechanically mixing for 2.5h, and then roasting for 5h under the conditions of helium atmosphere and 500 ℃, so as to obtain a solid sample for later use.
2) Dissolving 0.3g of 1-butyl-3-methylimidazolium hexafluorophosphate and 1.2g of 1-propyl-3-butylimidazolium tetrafluoroborate ionic liquid in 15mL of nitrogen alkyl pyrrolidone, stirring uniformly, adding the solid sample obtained in the step 1), soaking for 6h, and drying at 180 ℃ for later use. Wherein the mass loading of the ionic liquid is 15%.
3) Dissolving 0.2g of rhodium chloride in 1.6mL of nitrogen methyl pyrrolidone, stirring uniformly, adding the sample obtained in the step 2), soaking in an external 0.8kV static electric field for 3.5h, and drying at 180 ℃ for later use. Wherein the mass loading of rhodium element is 1.0%.
4) 11.6g of the solid sample obtained above was redispersed in 100mL of a mixed solution of azaalkylpyrrolidone and 0.5g of dimethyldichlorosilane. And the mixture obtained above was subjected to a rotary treatment on a rotary apparatus at 55 ℃ for 13 h. And then dipping the catalyst in an externally added 1.2kV static electric field for 4 hours, and drying the catalyst at 180 ℃ in an oxygen atmosphere to obtain the required solid catalyst.
Evaluation of catalyst Performance:
the catalyst 3.0g is applied to acetylene hydrochlorination reaction in a fixed bed reactor, and the reaction conditions are as follows: the temperature is 150 ℃, the pressure is 0.4MPa, and the mass ratio of the raw material gas substances n (HCl)/n (C)2H2) 1.2/1, acetylene volume space velocity of 80h-1Under the condition of (1), the induction period is 0h, and after 2000h of reaction, the acetylene conversion rate is 95% and the vinyl chloride selectivity is 97.5%.
Example 5
Preparation of the catalyst:
1) selecting 7.5g of copper substrate grapyne and 2.5g of aluminum-magnesium-boron powder, mechanically mixing for 3.5h, and then roasting for 6h under the conditions of nitrogen atmosphere and 600 ℃, wherein the obtained solid sample is reserved.
2) 0.3g of 1-butyl-3-methylimidazolium hexafluorophosphate and 0.7g of azomethylpyrrolidone hydrochloride are dissolved in 10mL of thionyl chloride, and after uniform stirring, the solid sample obtained in the step 1) is added, soaked for 7h and dried at 180 ℃ for later use. Wherein the mass loading of the ionic liquid is 10%.
3) Dissolving 4.23g of copper chloride in 2.12mL of thionyl chloride, stirring uniformly, adding the sample obtained in the step 2), soaking in an external 2.5kV static electric field for 4 hours, and drying at 180 ℃ for later use. Wherein the mass loading of the copper element is 20 percent.
4) 15.23g of the solid sample obtained above was redispersed in 300mL of a mixed solution of thionyl chloride and 1.5g of dimethyldichlorosilane. And the mixture obtained above was subjected to a spinning treatment for 14h at 60 ℃ on a spinner. And then dipping the catalyst in an externally added 1.8kV static electric field for 3.5h, and drying the catalyst at 180 ℃ in an air atmosphere to obtain the required solid catalyst.
Evaluation of catalyst Performance:
1.5g of the catalyst is applied to acetylene hydrochlorination in a fixed bed reactor, and the reaction conditions are as follows: temperature 160 ℃, pressure 0.5MPa, ratio of the amount of the raw material gas substances n (HCl)/n (C)2H2) 0.9/1, and the space velocity of acetylene volume is 50h-1Under the condition of (1), the induction period is 0h, and after the reaction is 2000h, the acetylene conversion rate is 98 percent and the chloroethylene selectivity is 96.5 percent.
Example 6
Preparation of the catalyst:
1) selecting 0.91g of graphite alkyne powder and 9.1g of aluminum-magnesium-boron powder, mechanically mixing for 4 hours, and then roasting for 8 hours under the conditions of argon atmosphere and 800 ℃, so as to obtain a solid sample for later use.
2) Dissolving 1-butyl-2, 3-dimethyl imidazole tetrafluorophosphate and 1g triphenyl ethyl phosphine bromide ionic liquid in 200mL of acetone, stirring uniformly, adding the solid sample obtained in the step 1), soaking for 10h, and drying at 180 ℃ for later use. Wherein the mass loading of the ionic liquid is 10%.
3) Dissolving 2.5g of copper sulfate in 10mL of acetone, stirring uniformly, adding the sample obtained in the step 2), soaking for 2 hours in an external 0.9kV static electric field, and drying at 180 ℃ for later use. Wherein the mass loading of the copper element is 10 percent.
4) 14.5g of the solid sample obtained above was redispersed in a mixed solution of 500mL of acetone and 1.25g of dimethyldichlorosilane. And the mixture obtained above was subjected to a spinning treatment for 12h at 50 ℃ on a spinner. And then dipping the catalyst in an externally added 1.5kV static electric field for 2h, and drying the catalyst at 180 ℃ in a nitrogen atmosphere to obtain the required solid catalyst.
Evaluation of catalyst Performance:
the catalyst 3.0g is applied to acetylene hydrochlorination reaction in a fixed bed reactor, and the reaction conditions are as follows: the temperature is 200 ℃, the pressure is 0.1MPa, and the mass ratio of the raw material gas substances n (HCl)/n (C)2H2) 1.2/1, acetylene volume space velocity of 30h-1Under the condition of (1), the induction period is 0h, and after the reaction is 2000h, the acetylene conversion rate is 98 percent and the chloroethylene selectivity is 99.5 percent.
Comparative example 1
This comparative example investigated the effect of metal dispersion in the ionic liquid layer on catalytic performance by comparison with example 1.
Preparation of the catalyst:
dissolving 0.08g of triphenylphosphine bis (trifluoromethanesulfonyl) imide salt and 0.02g of triphenylphosphine ethyl bromide ionic liquid in 10mL of deionized water solution, adding 9.1g of graphite alkyne film and 0.91g of aluminum-magnesium-boron powder, mechanically mixing for 3h, and roasting for 2h at 200 ℃ in a nitrogen atmosphere to obtain a solid sample for later use. Then adding a certain content of chloroauric acid solution. After dipping for 3h, drying at 110 ℃ for standby. Wherein the mass loading amounts of the gold element and the ionic liquid are respectively 0.05 percent and 1 percent.
Evaluation of catalyst Performance:
the catalyst is applied to acetylene hydrochlorination in a fixed bed reactor, and the reaction conditions are as follows: the temperature is 140 ℃, the pressure is 0.3MPa, and the raw materialsThe ratio of the amounts of gaseous substances n (HCl)/n (C)2H2) 1.2/1, acetylene volume space velocity of 50h-1Under the condition of (1), the induction period is 3h, and after 2000h of reaction, the acetylene conversion rate is 76% and the vinyl chloride selectivity is 99.0%.
Comparative example 2
This comparative example studies the effect of metal anchoring to the support surface and then covering with a layer of ionic liquid on the catalytic performance by comparison with example 1.
And (3) mechanically mixing 9.1g of the graphdine film and 0.91g of aluminum-magnesium-boron powder for 3 hours, and then roasting for 2 hours at 200 ℃ in a nitrogen atmosphere to obtain a solid sample for later use. Then adding a certain content of chloroauric acid solution. After dipping for 3h, drying at 110 ℃ for standby. Wherein the mass loading of the gold element is 0.05 percent. To the dried ready sample, 0.08g of triphenylphosphine bistrifluoromethylsulfonyl imide salt, 0.02g of triphenylphosphine ethyl phosphonium ionic liquid and 10mL of deionized water were added. After being stirred evenly, the mixture is dried for standby at the temperature of 110 ℃. Wherein the mass loading amounts of the gold element and the ionic liquid are respectively 0.05 percent and 1 percent.
Evaluation of catalyst Performance:
the catalyst is applied to acetylene hydrochlorination in a fixed bed reactor, and the reaction conditions are as follows: the temperature is 140 ℃, the pressure is 0.3MPa, and the mass ratio of the raw material gas substances n (HCl)/n (C)2H2) 1.2/1, acetylene volume space velocity of 50h-1Under the condition of (1), the induction period is 8 hours, and after 2000 hours of reaction, the acetylene conversion rate is 57 percent and the vinyl chloride selectivity is 98.9 percent.

Claims (10)

1. An aluminum-magnesium-boron powder/graphite alkyne mixed carrier loaded metal catalyst is characterized by being prepared by the following method:
(1) mechanically mixing a graphite alkyne carrier with aluminum-magnesium-boron powder for 2-5 hours, and then roasting for 2-8 hours at 200-800 ℃ in an inert gas atmosphere to obtain a mixed carrier;
(2) dissolving ionic liquid in a solvent, uniformly stirring, adding the mixed carrier obtained in the step (1), soaking for 2-10 hours, and drying to obtain a solid product loaded with the ionic liquid;
the mass ratio of the ionic liquid to the mixed carrier is 1-20: 100, respectively;
the ionic liquid is selected from one or a mixture of more than two of the following formulas (I) to (V) in any proportion;
Figure FDA0002593957460000011
in the formula (I), the compound is shown in the specification,
R1is H, CH3Or C2H5；
R2Is CnH2n+1N is an integer and n is not less than 1 and not more than 14;
R3is CkH2k+1K is an integer and is not less than 1 and not more than 4;
X-is chloride ion, bromide ion, hexafluorophosphate radical, tetrafluorophosphate radical, bis (trifluoromethanesulfonyl) imide radical or tetrafluoroborate radical;
Figure FDA0002593957460000012
in the formula (II), the compound is shown in the specification,
R1、R2、R3、R4each independently is CnH2n+1N is an integer and n is not less than 1 and not more than 6;
X-is chloride ion, bromide ion, hexafluorophosphate radical, tetrafluorophosphate radical, bis (trifluoromethanesulfonyl) imide radical or tetrafluoroborate radical;
Figure FDA0002593957460000013
in the formula (III), the compound represented by the formula (III),
R1、R2、R3、R4each independently is CnH2n+1N is an integer and n is not less than 1 and not more than 6;
X-is chloride ion, bromide ion, hexafluorophosphate radical, tetrafluorophosphate radical, bis (trifluoromethanesulfonyl) imide radical or tetrafluoroborate radical;
Figure FDA0002593957460000014
in the formula (IV), the compound is shown in the specification,
R1、R2each independently is CnH2n+1N is an integer and n is not less than 1 and not more than 6;
R3is CnH2n+1Sulfur or oxygen atoms, n is an integer and n is greater than or equal to 1 and less than or equal to 6;
X-is chloride ion, bromide ion, hexafluorophosphate radical, tetrafluorophosphate radical, bis (trifluoromethanesulfonyl) imide radical or tetrafluoroborate radical;
Figure FDA0002593957460000021
in the formula (V), the compound represented by the formula (V),
R1、R2each independently is CnH2n+1N is an integer and n is not less than 1 and not more than 6;
R3is CnH2n+1Sulfur or oxygen atoms, n is an integer and n is greater than or equal to 1 and less than or equal to 6;
X-is chloride ion, bromide ion, hexafluorophosphate radical, tetrafluorophosphate radical, bis (trifluoromethanesulfonyl) imide radical or tetrafluoroborate radical;
alternatively, the ionic liquid is selected from one of the following:
the mass ratio of the triphenylphosphine bistrifluoromethanesulfonimide salt to the triphenylphosphine ethyl bromide is 4: 1;
the mass ratio of the triphenylphosphine bistrifluoromethanesulfonimide salt to the N-amyl-ethylpiperidine chloride salt is 1: 1;
the mass ratio of 1-butyl-2, 3-dimethyl imidazole tetrafluorophosphate to triphenyl ethyl phosphine bromide is 1: 1;
the mass ratio of the 1-butyl-3-methylimidazole hexafluorophosphate to the N-methylpyrrolidone hydrochloride is 3: 7;
(3) dissolving metal salt in a solvent, uniformly stirring, adding the ionic liquid loaded solid product obtained in the step (2), soaking in an external static electric field for 2-4 h, and then drying for later use;
the mass ratio of metal elements contained in the metal salt to the mixed carrier is 0.05-20: 100, respectively;
the metal salt can be marked as MX, wherein M is a metal cation and is selected from one or more of gold, ruthenium, rhodium and copper, and X is a non-metal anion and is selected from one or more of nitrate, sulfate, chlorine, bromine, dicyandiamide radical, thiosulfate radical, sulfite radical, phosphate radical, pyrophosphate radical, poly-phthalocyanine radical, phthalocyanine radical and dichloro (1, 10-phenanthroline) radical;
(4) dispersing the product obtained in the step (3) in a mixed solution of a solvent and dimethyldichlorosilane, then placing the mixture on a rotary mixer for rotary treatment for 10-14 h at 40-60 ℃, then dipping the mixture in an external static electric field for 2-4 h, and drying the mixture in a specific atmosphere to obtain the aluminum-magnesium-boron powder/graphite alkyne mixed carrier supported metal catalyst;
in the mixed solution of the solvent and the dimethyldichlorosilane, the ratio of the volume of the solvent in mL to the mass of the dimethyldichlorosilane in g is 50-400: 1;
the specific atmosphere is selected from one or a mixture of several of nitrogen, argon, air, oxygen, hydrogen, acetylene, hydrogen chloride, methane, oxygen and chlorine.
2. The aluminum-magnesium-boron powder/graphite alkyne mixed carrier supported metal catalyst of claim 1, wherein in the step (1), the mass ratio of the graphite alkyne carrier to the aluminum-magnesium-boron powder is 1: 0.1 to 10.
3. The aluminum-magnesium-boron powder/graphdine mixed carrier supported metal catalyst according to claim 1, wherein in the step (2), the solvent is one or a mixture of two or more of toluene, N-dimethylformamide, N-alkylpyrrolidone, thionyl chloride and acetone in any proportion, and the solvents used in the steps (3) and (4) are the same as those used in the step (2).
4. The aluminum-magnesium-boron powder/graphdiyne mixed carrier supported metal catalyst of claim 1, wherein in the step (2), the volume usage of the solvent is 5-100 mL/g based on the mass of the ionic liquid.
5. The aluminum-magnesium-boron powder/graphdine mixed carrier supported metal catalyst of claim 1, wherein in step (2), the ionic liquid is selected from one of the following:
the mass ratio of the triphenylphosphine bistrifluoromethanesulfonimide salt to the triphenylphosphine ethyl bromide is 4: 1;
the mass ratio of the triphenylphosphine bistrifluoromethanesulfonimide salt to the N-amyl-ethylpiperidine chloride salt is 1: 1;
the mass ratio of the 1-propyl-2, 3-dimethyl imidazole bistrifluoromethane sulfimide salt to the 1-hexyl-2, 3-dimethyl imidazole bistrifluoromethane sulfimide salt is 1: 1;
the mass ratio of 1-butyl-3-methylimidazole hexafluorophosphate to 1-propyl-3-butylimidazole tetrafluoroborate is 1: 4;
the mass ratio of the 1-butyl-3-methylimidazole hexafluorophosphate to the N-methylpyrrolidone hydrochloride is 3: 7;
the mass ratio of 1-butyl-2, 3-dimethyl imidazole tetrafluorophosphate to triphenyl ethyl phosphine bromide is 1: 1.
6. The aluminum-magnesium-boron powder/graphdiyne mixed carrier supported metal catalyst of claim 1, wherein in the step (3), the volume usage of the solvent is 0.5-10 mL/g based on the mass of the metal salt.
7. The aluminum-magnesium-boron powder/graphdiyne mixed carrier supported metal catalyst of claim 1, wherein in the step (4), the volume usage of the mixed solution of the solvent and the dimethyldichlorosilane is 5 to 60mL/g based on the mass of the product obtained in the step (3).
8. The aluminum-magnesium-boron powder/graphite alkyne mixed carrier supported metal catalyst of claim 1, wherein in the step (3) or (4), the voltage of the applied static electric field is 0.2-4 kV.
9. The use of the Al-Mg-B powder/graphite alkyne mixed carrier supported metal catalyst of claim 1 in the reaction of synthesizing vinyl chloride by calcium carbide process.
10. The application of claim 9, wherein the method of applying is:
the prepared catalyst is filled in a fixed bed reactor, the reaction temperature is 100-200 ℃, the reaction pressure is 0.1-0.5 MPa, and raw material gases HCl and C are introduced2H2Then vinyl chloride can be obtained through reaction;
the raw material gases are HCl and C2H2The ratio of the amounts of substances n (HCl)/n (C)2H2) 0.9-1.2/1; the volume space velocity of acetylene is 10-100 h-1。
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