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pt/α-moc 1-x Application of Supported Catalysts in Catalytic Hydrogenation

A supported catalyst, -moc1-x technology, applied in physical/chemical process catalysts, preparation of organic compounds, organic chemistry, etc., can solve problems such as increasing the cost of catalytic hydrogenation reactions

Active Publication Date: 2020-04-17
PEKING UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

According to the U.S. Department of Energy’s Renewable Energy National Laboratory (NERL) report (NREL / SR-540-32525): According to the different sources of hydrogen, the investment in fixed assets and daily operating costs required to purify hydrogen by pressure swing adsorption accounted 10-20% of the total production cost; it can be seen that the production cost of high-purity hydrogen is significantly higher than that of crude hydrogen; and the use of high-purity hydrogen increases the cost of industrial catalytic hydrogenation reactions

Method used

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  • pt/α-moc  <sub>1-x</sub> Application of Supported Catalysts in Catalytic Hydrogenation
  • pt/α-moc  <sub>1-x</sub> Application of Supported Catalysts in Catalytic Hydrogenation
  • pt/α-moc  <sub>1-x</sub> Application of Supported Catalysts in Catalytic Hydrogenation

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0061] Preparation of carrier α-MoC 1-x

[0062] Grind 1g of molybdenum trioxide to less than 60 mesh, place it in a quartz tube, program the temperature to 700°C in an ammonia gas reaction atmosphere, keep it for 1 hour, and then cool it down to room temperature in an ammonia gas reaction atmosphere; wherein, the heating rate is 10 °C / min, the flux of ammonia gas is 20mL / min;

[0063] Switch the reaction atmosphere to methane and hydrogen, program the temperature to 700°C, keep it for 1 hour, and then cool down to room temperature in the atmosphere of methane and hydrogen; wherein, the heating rate is 10°C / min, and the flux of methane and hydrogen is 20mL / Minutes, the volume ratio of methane and hydrogen is 3:7;

[0064] Switch the reaction atmosphere to a passivation atmosphere, program the temperature to 700°C, keep it for 1 hour, and then cool it down to room temperature in the passivation atmosphere; wherein, the heating rate is 10°C / min, and the flux of the passivatio...

Embodiment 2

[0066] Pt / α-MoC with 0.2% loading 0.8 Supported catalyst (referred to as 0.2%Pt / α-MoC 0.8 )Synthesis

[0067] The carrier α-MoC prepared by the method of Example 1 0.8 (0.2g) was put into a flask, and 10mL of deionized water was added to make the carrier all under the liquid surface. Dissolve 1 g of the platinum precursor salt chloroplatinic acid hexahydrate in 10 mL of water to prepare a Pt solution; take 25 μL of the Pt solution and add it to the carrier α-MoC 0.8 The flask was stirred for 2 hours, the water in the flask was evaporated with a rotary evaporator, and then the sample was placed in a freeze dryer to freeze-dry overnight. Then the catalyst precursor was in CH 4 / H 2 Carbonization in an atmosphere (the volume ratio of methane to hydrogen is 3:17), the temperature is raised to 300°C at a rate of 10°C / min, kept at 300°C for one hour, and then raised to 590°C at a rate of 10°C / min, and Leave on for 120 minutes. Finally, the loading was determined to be about 0...

Embodiment 3

[0069] Pt / α-MoC with 0.5% loading 0.8 Supported catalyst (referred to as 0.5%Pt / α-MoC 0.8 )Synthesis

[0070] The carrier α-MoC prepared by the method of Example 1 0.8 (0.2g) was put into a flask, and 10mL of deionized water was added to make the carrier all under the liquid surface. Dissolve 1 g of the platinum precursor salt chloroplatinic acid hexahydrate in 10 mL of water to prepare a Pt solution; take 25 μL of the Pt solution and add it to the carrier α-MoC 0.8 After stirring for 2 hours, the water in the flask was evaporated with a rotary evaporator, and then the sample was placed in a freeze dryer to freeze-dry overnight. Then the catalyst precursor was in CH 4 / H 2 Carbonization in an atmosphere (the volume ratio of methane to hydrogen is 3:17), the temperature is raised to 300°C at a rate of 10°C / min, kept at 300°C for 1 hour, and then raised to 590°C at a rate of 10°C / min, And keep it for 120 minutes. The loading was finally determined to be about 0.5% by ICP....

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Abstract

The embodiment of the invention provides an application of a Pt / alpha-MoC<1-x> supported catalyst in catalytic hydrocracking reaction. A hydrogen source gas for providing a nitrogen element for catalytic hydrocracking reaction comprises CO, wherein the volume percentage of the CO is greater than 0.01%. According to the Pt / alpha-MoC<1-x> supported catalyst, alpha-MoC<1-x> is taken as a carrier, Pt is taken as an active component, and 1-100% of Pt is dispersed into the carrier alpha-MoC<1-x> in a monatomic form. When the Pt / alpha-MoC<1-x> supported catalyst is applied to catalytic hydrocracking reaction, the volume percentage of the CO contained in the hydrogen source gas can be greater than 0.01%. Therefore, catalytic hydrocracking reaction can be carried out by adopting crude hydrogen with relatively high CO content, thereby reducing the cost of catalytic hydrocracking reaction.

Description

technical field [0001] The invention relates to the technical field of catalytic hydrogenation, in particular to Pt / α-MoC 1-x Application of supported catalysts in catalytic hydrogenation reactions. Background technique [0002] Catalytic hydrogenation reaction refers to the chemical reaction process in which unsaturated organic matter and hydrogen gas generate corresponding saturated organic compounds under the action of a catalyst, which belongs to the category of reduction reaction. Platinum (Pt for short) has been used as a catalyst in various catalytic hydrogenation reactions, but it still has two problems as a catalyst for catalytic hydrogenation reactions: [0003] On the one hand, due to the extremely strong hydrogenation performance of Pt, in compounds containing multiple hydrogenation functional groups (such as -C=C, -C≡C, -C=O, -C≡N, -NO 2 etc.) will hydrogenate all functional groups non-selectively. [0004] On the other hand, Pt is easily poisoned by carbon m...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/22C07C209/36C07C221/00C07C211/45C07C211/52C07C223/06
CPCB01J27/22C07C209/36C07C209/365C07C221/00C07C211/45C07C211/52C07C223/06
Inventor 马丁林丽利姚思宇
Owner PEKING UNIV