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Ionic liquid catalytic deoxygenation method in a lignin derivative hydrodeoxygenation process

An ionic liquid, hydrodeoxygenation technology, applied in physical/chemical process catalysts, chemical instruments and methods, chemical/physical processes, etc., can solve problems such as restricting applications, and achieve the advantages of overcoming high pressure problems, easy separation, and avoiding side reactions. Effect

Active Publication Date: 2021-02-19
INST OF PROCESS ENG CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, under the reported process conditions, phosphoric acid is still an essential part as a deoxidizer in the reaction process, which also seriously restricts its application in industrial production.

Method used

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  • Ionic liquid catalytic deoxygenation method in a lignin derivative hydrodeoxygenation process
  • Ionic liquid catalytic deoxygenation method in a lignin derivative hydrodeoxygenation process
  • Ionic liquid catalytic deoxygenation method in a lignin derivative hydrodeoxygenation process

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Experimental program
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Effect test

Embodiment 1

[0026] Ionic liquid synthesis: equimolar amounts of alkanolamine (5mol) and trifluoromethanesulfonic acid (5mol) were added to a round bottom flask and a constant pressure titration funnel, respectively, and 500 mL of methanol was added to the round bottom flask as a reaction solvent. Under the condition of ice water temperature, trifluoromethanesulfonic acid was slowly added dropwise to the methanol solution of alcoholamine. After the dropwise addition was completed, the reaction system was warmed up to room temperature (25°C) and reacted for 24 hours to remove methanol to obtain the target ion liquid.

[0027] The ionic liquids used in the following cases were all synthesized by the above method.

[0028] 1mmol phenol, 0.1g Rh / C (water content 55-60%) catalyst, 2g N-methyldiethanolamine trifluoromethanesulfonate ([BHEM][OTf]) ionic liquid, 1mmol n-dodecane and Magnets are added to a stainless steel autoclave with a Teflon liner and tightly sealed. Then use high-purity hydr...

Embodiment 2

[0030] 1mmol cyclohexanol, 0.1g Pt / C (water content≤80%) catalyst, 2g N-methyldiethanolamine trifluoromethanesulfonate [BHEM][OTf] ionic liquid, 1mmol n-dodecane and magnetic Pour into a stainless steel autoclave lined with polytetrafluoroethylene, and seal it tightly. Then use high-purity hydrogen to pump and vent the reactor three times to blow out the air in the reactor, and inject 4MPa hydrogen into the reactor after the last ventilation. Put the reaction kettle into the high-pressure reaction furnace, wait until the temperature is heated to the set temperature of 120°C, turn on the magnetic stirring and set the magnetic stirring speed to 550 rpm, and start timing. After reacting for 2 hours, the reaction kettle was put into ice water for cooling. After complete cooling, slowly release the remaining high-pressure hydrogen in the reactor, and blow the hydrogen in the reactor with nitrogen, then open the reactor, and extract the reaction product with 8ml of methyl tert-buty...

Embodiment 3

[0032]1mmol phenol, 0.1g Rh / C (water content 55-60%) catalyst, 2g N,N-dimethylethanolamine trifluoromethanesulfonate ([2-HTEAF][OTf]) ionic liquid, 0.1910g Add n-dodecane and magnetons into a stainless steel autoclave with a polytetrafluoroethylene liner, and tighten the seal. Then use high-purity hydrogen to pump and vent the reactor three times to blow out the air in the reactor, and inject 4MPa hydrogen into the reactor after the last ventilation. Put the reaction kettle into the high-pressure reaction furnace, wait until the temperature is heated to the set temperature of 120°C, turn on the magnetic stirring and set the magnetic stirring speed to 550 rpm, and start timing. After reacting for 10 hours, the reaction kettle was put into ice water for cooling. After complete cooling, slowly release the remaining high-pressure hydrogen in the reactor, and blow the hydrogen in the reactor with nitrogen, then open the reactor, and extract the reaction product with 8ml of methyl ...

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Abstract

The invention discloses a method for preparing high calorific value alkanes by catalytic deoxygenation of ionic liquid in the hydrogenation deoxygenation reaction of aromatic compounds derived from lignin. The method selects a proton-type ionic liquid catalyst whose anion is trifluoromethanesulfonic acid, and is characterized in that: under the conditions of temperature 100-150°C, hydrogen pressure 1-5MPa, and time 2-20 hours, the ionic liquid is realized in a batch kettle. Liquid-catalyzed efficient deoxygenation process of lignin-derived aromatic compounds to efficiently produce biomass alkane gasoline. The method has mild reaction conditions, low energy consumption, good thermal stability of the catalyst, high product cycloalkane selectivity, lignin derivative conversion rate of 100%, and product cycloalkane selectivity as high as 98%. The method avoids the addition of protonic acid in the conventional catalytic system, and the extremely low vapor pressure of the ionic liquid ensures that the reaction system maintains a low pressure, reducing the requirements for equipment. At the same time, the ionic liquid used in the process is easy to separate from the product, the catalytic system has good cycle performance, and has good potential for industrial application.

Description

technical field [0001] The invention relates to a method for preparing high-calorific-value biomass oil by catalytically converting lignin-derived aromatic compounds in a hydrodeoxygenation reaction under mild conditions based on ionic liquid as a catalyst, and belongs to the field of utilization of biomass resources. Background technique [0002] With the depletion of petrochemical resources and people's higher and higher environmental requirements, it is becoming increasingly important to develop new technologies to utilize renewable green resources. Due to its high reserves, wide distribution, recyclability and non-polluting characteristics, biomass resources have gradually attracted people's attention. Therefore, efficient utilization of biomass energy has become one of the best ways to solve energy problems and environmental pollution. The composition of woody biomass resources mainly includes cellulose (35-55%), hemicellulose (20-35%) and lignin (15-30%). According to...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C1/22C07C13/18B01J31/02
Inventor 张锁江周清蔡光明杨绍旗李晓前吕兴梅
Owner INST OF PROCESS ENG CHINESE ACAD OF SCI