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Method for preparing alkane through lignin derivative in ionic liquid system

A technology of ionic liquid and lignin, which is applied in the preparation of liquid hydrocarbon mixtures, biological raw materials, petroleum industry, etc., can solve the problems of high pressure and achieve the effects of improving the utilization rate of metals, avoiding reactions, and high selectivity

Active Publication Date: 2019-02-01
INST OF PROCESS ENG CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, in this volatile solvent system, since the reaction process requires a higher temperature, the volatilization of the solvent results in a higher pressure in the reaction system, which also puts forward very high requirements on the equipment.

Method used

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  • Method for preparing alkane through lignin derivative in ionic liquid system
  • Method for preparing alkane through lignin derivative in ionic liquid system
  • Method for preparing alkane through lignin derivative in ionic liquid system

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Experimental program
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Effect test

Embodiment 1

[0026] Adopt the Ru / SBA-15 of 5wt% in this embodiment as catalyst, its preparation method is as follows:

[0027] Weigh 0.25g of ruthenium chloride (Ru 40%) and dissolve it in 20mL of deionized water, add the aqueous solution of ruthenium chloride to 2g of SBA-15 molecular sieve, and stir evenly with a glass rod. After mixing, it was placed in a blast drying oven at 100°C for 10 hours. Then the loaded metal salt was placed in a tube furnace under an argon atmosphere and calcined at 500° C. for 5 hours, and then cooled naturally. Finally, the gas atmosphere was changed, calcined at 500° C. for 4 hours under the condition of hydrogen, and cooled naturally to obtain the target catalyst. The preparation methods of other metal catalysts are similar to the above methods.

[0028] Carry out the hydrodeoxygenation experiment concrete operation steps of phenol in ionic liquid solvent system as follows:

[0029] Add 1mmol of phenol, 0.1g of catalyst Ru / SBA-15, 2g of ionic liquid, 0.1...

Embodiment 2

[0034] In this example, 5 wt% of Ru / SBA-15, Ir / SBA-15, Rh / SBA-15, Pt / SBA-15, Ru / C, Ru / SiO 2 , Re / SBA-15, Pd / SBA-15 and Ru / γ-Al 2 o 3 As a catalyst, in the ionic liquid [Bmim]PF 6 The specific operation steps of the hydrodeoxygenation experiment of diphenyl ether in the solvent system are as follows:

[0035] 1mmol diphenyl ether, 0.1g catalyst, 2g ionic liquid [Bmim]PF 6 , 0.1735g of n-dodecane and magnetons were added into a stainless steel autoclave with polytetrafluoroethylene lining, and sealed. Introduce high-purity hydrogen to ventilate the reactor for 3 times to evacuate the air in the reactor, and inject 2MPa high-purity hydrogen. The reaction kettle was put into a high-pressure reaction furnace and heated to 130° C., and reacted for 6 hours with a stirring rate of 600 rpm. After the reaction is over, put the reaction kettle into the ice-water mixture to quench and condense for 2 hours, empty the hydrogen in the kettle and sweep it with nitrogen to completely remo...

Embodiment 3

[0040] Add 1 mmol guaiacol, 0.1 g catalyst Ir / SBA-15, 2 g ionic liquid [Bmim] PF6, 0.1735 g n-dodecane and magnetons into a stainless steel autoclave with Teflon liner, seal . Introduce high-purity hydrogen to ventilate the reactor for 3 times to evacuate the air in the reactor, and inject 2MPa high-purity hydrogen. The reaction kettle was put into a high-pressure reaction furnace and heated to 130° C., and reacted for 6 hours with a stirring rate of 600 rpm. After the reaction is over, put the reaction kettle into the ice-water mixture to quench and condense for 2 hours, empty the hydrogen in the kettle and sweep it with nitrogen to completely remove the hydrogen, open the reaction kettle, and extract the reaction with 8mL methyl tert-butyl ether product. The obtained products were analyzed qualitatively and quantitatively by gas chromatography-mass spectrometry (GC-MS) and gas phase analyzer (GC). The analysis results showed that the conversion rate of guaiacol was 100%, ...

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Abstract

The invention discloses a method for preparing a high calorific value alkane by one-step hydrodeoxygenation of a lignin-derived aromatic compound in an ionic liquid system. The method adopts a transition metal supported catalyst and is characterized in that biomass alkane gasoline is prepared through lignin-derived compound high-efficiency hydrodeoxygenation in an intermittent reactor at 100-160 DEG C under hydrogen gas pressure of 1-5MPa for 2-10h. The catalytic system has mild reaction conditions and low energy consumption. The catalyst has good dispersibility in the ionic liquid. The ligninderivative conversion rate is 100%. The selectivity of the product cycloalkane is 95% or more. The method is free of protonic acid in the conventional catalytic system. The extremely low vapor pressure of the ionic liquid keeps the system low pressure during the reaction process, the requirements on the equipment are reduced, cycle performances of the catalytic system are good, and the method hasgood industrial application prospects.

Description

technical field [0001] The invention relates to a method for preparing high-calorific-value biomass alkane gasoline by catalytically converting lignin derivatives under mild conditions with a catalytic system established based on ionic liquids and supported metal catalysts, and belongs to the field of utilization of biomass resources. Background technique [0002] As human beings have higher and higher requirements for the living environment, the development and utilization of green and recyclable resources has attracted widespread attention. Biomass resources are green renewable energy with large reserves and wide distribution on the earth. The development and efficient utilization of biomass resources is one of the keys to realize the adjustment of human energy structure. Biomass resources are mainly composed of three components: cellulose (35-55%), hemicellulose (20-35%) and lignin (15-30%). Different components can be extracted by biomass separation technology and take ...

Claims

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Application Information

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IPC IPC(8): C10G3/00
CPCC10G3/49C10G3/52Y02P30/20
Inventor 吕兴梅杨绍旗徐俊丽姚浩余康莹杨永青辛加余张锁江
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI