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Method for preparing alkane through hydrodeoxygenation of oxygen-containing organic compounds

An organic compound and hydrodeoxygenation technology, which is applied in the preparation of liquid hydrocarbon mixtures, biological raw materials, petroleum industry, etc., can solve the problems of increasing catalyst manufacturing costs and reducing catalysts, achieving good industrial application prospects, reducing manufacturing costs, and mature production effect of technology

Active Publication Date: 2019-08-13
UNIV OF SCI & TECH OF CHINA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Although the relatively mild reaction conditions are indeed conducive to the realization of industrial production, the expensive rare earth metal niobium and the complex niobium oxyphosphate (NbOPO 4 ) carrier preparation technology has significantly increased the manufacturing cost of the catalyst, which will also greatly reduce the possibility of using niobium oxyphosphate as a carrier catalyst for industrial production

Method used

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  • Method for preparing alkane through hydrodeoxygenation of oxygen-containing organic compounds
  • Method for preparing alkane through hydrodeoxygenation of oxygen-containing organic compounds
  • Method for preparing alkane through hydrodeoxygenation of oxygen-containing organic compounds

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0059] Example 1: Preparation of alkanes by hydrodeoxygenation of different oxygen-containing organic compounds as raw materials

[0060] In a 25mL autoclave, add 1mmol of the oxygen-containing organic compounds shown in Table 1 below, 100mg 2 The Ru content after the pre-reduction treatment is a supported Ru catalyst (3%Ru / Ca 5 (PO 4 ) 3 (OH)) and 10mL hexanaphthene as solvent, then close the reactor and replace it with hydrogen, heat to 180°C under 4MPa hydrogen atmosphere, and react under mechanical stirring for the time shown in Table 1. After the reaction was completed, the reaction was cooled to room temperature and degassed to reduce pressure, the reaction kettle was opened, the reaction solution was washed out with cyclohexane, the catalyst and the reaction solution were separated by centrifugation, and the obtained reaction solution was analyzed by gas chromatography.

[0061] The gas chromatography conditions are as follows: GC99 gas chromatography, FID detector, ...

Embodiment 2

[0068] Embodiment 2: the investigation of reaction temperature and hydrogen pressure

[0069] In a 25mL autoclave, add 1mmol of the oxygen-containing organic compound of formula I, 100mg of H 2 The Ru content after the pre-reduction treatment is a supported Ru catalyst (3%Ru / Ca 5 (PO 4 ) 3 (OH)) and 10mL hexanaphthene as solvent, then closed reactor and after replacing with hydrogen, under the temperature shown in Table 2 and hydrogen pressure, under mechanical stirring, react the time shown in Table 2. After the reaction was completed, the reaction was cooled to room temperature and degassed and decompressed, the reactor was opened, the reaction solution was washed out with hexanaphthene, the catalyst and the reaction solution were separated by centrifugation, and the reaction solution obtained by gas chromatography analysis, wherein The gas chromatography conditions are the same as in Example 1, and the results are shown in Table 2.

[0070] Table 2: Investigation result...

Embodiment 3

[0074] Example 3: Investigation of different active metals or different apatite carriers

[0075] In a 25mL autoclave, add 1mmol of the oxygen-containing organic compound of formula I, 100mg of H 2 The loaded metal catalyst shown in the following table 3 after pre-reduction treatment (wherein the content of active metal is 3% by weight) and 10mL hexanaphthene are used as solvent, then after closing the reactor and replacing it with hydrogen, feed 4MPa hydrogen and Heated to 180°C and reacted for 12 hours under mechanical stirring. After the reaction was completed, the reaction was cooled to room temperature and degassed and decompressed, the reactor was opened, the reaction solution was washed out with hexanaphthene, the catalyst and the reaction solution were separated by centrifugation, and the reaction solution obtained by gas chromatography analysis, wherein The gas chromatography conditions are the same as in Example 1, and the results are shown in Table 3.

[0076] Tab...

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Abstract

The invention relates to a method for preparing alkane through hydrodeoxygenation of oxygen-containing organic compounds. The method comprises the step of making the oxygen-containing organic compounds subjected to a hydrodeoxygenation reaction in a hydrogen atmosphere in the presence of a hydrodeoxygenation catalyst to obtain corresponding alkane products in one step. By utilizing a specific supported metal catalyst or a mixed catalyst of the supported metal catalyst and an acid catalyst, the oxygen-containing organic compounds such as alcohols, aldehydes, esters, ethers, ketones and acids can be completely subjected to hydrodeoxygenation in one step under the mild conditions of lower temperature and lower pressure in the presence or absence of a solvent, and the corresponding alkane products can be obtained with a high conversion rate and a high yield. Meanwhile, the method has the advantages of short reaction flow, simple reaction equipment and low catalyst cost and is suitable forindustrial production.

Description

technical field [0001] The invention relates to a method for preparing alkanes by hydrodeoxygenation of oxygen-containing organic compounds. Background technique [0002] Facing the current situation of dwindling fossil energy reserves, building an energy security strategy is a basic requirement for achieving sustainable social development. In this context, the sustainable supply of hydrocarbon fuels is a major challenge, as the transport sector is the largest single consumer of crude oil. At present, hydrocarbon fuels are mainly produced from fossil resources (coal and petroleum). Coal and petroleum are non-renewable energy sources. Synthesizing hydrocarbon fuels from them will produce a large amount of carbon dioxide during the production and use process, resulting in a greenhouse effect. And in recent years, with the decrease of oil resources, the price of crude oil keeps rising, which makes the price of hydrocarbon fuels also rise steadily. Therefore, finding a renewab...

Claims

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Application Information

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IPC IPC(8): C10G3/00
CPCC10G3/44C10G3/48C10G3/49C10G3/50C10G3/60Y02P30/20
Inventor 张颖李奎许光月
Owner UNIV OF SCI & TECH OF CHINA