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A kind of preparation method of cycloalkane and aromatic hydrocarbon for aviation kerosene

A technology for aviation kerosene and naphthenic hydrocarbon, which is applied in the field of aviation kerosene and can solve the problems of low density and volume calorific value, poor sealing performance, etc.

Active Publication Date: 2019-07-19
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Compared with traditional aviation kerosene (a mixture of cyclic hydrocarbons and chain hydrocarbons), it has the disadvantages of lower density and volume calorific value and poor sealing performance

Method used

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  • A kind of preparation method of cycloalkane and aromatic hydrocarbon for aviation kerosene
  • A kind of preparation method of cycloalkane and aromatic hydrocarbon for aviation kerosene
  • A kind of preparation method of cycloalkane and aromatic hydrocarbon for aviation kerosene

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Experimental program
Comparison scheme
Effect test

Embodiment 1-20

[0034] 1. Preparation of catalyst:

[0035] 1) Preparation of metal catalyst:

[0036] Raney Ni, Raney Co, and Raney Cu are commercial catalyst products purchased directly; nickel-aluminum hydrotalcite (NiAl-HT) is Ni(NO 3 ) 2 ·6H 2 O and Al(NO 3 ) 3 9H 2 O mixed solution was added dropwise with NaOH and NaCO at 3mL / min 3 In the mixed solution, the dropwise addition process was carried out under strong stirring in a water bath at 65°C. After the dropwise addition, continue to stir and age for 18 hours, then filter and wash, dry at 80°C overnight, and restore at 500°C for 2 hours before use.

[0037] The steps of the catalyst prepared by the formaldehyde liquid phase reduction method are as follows: ultrasonically disperse one or more than two types of carriers with water, drop a metal precursor solution with a weight percentage of 2%-40% at room temperature, stir for 1 hour; Add NaOH solution to adjust the pH value to 9-10; add excess formaldehyde solution while stirri...

Embodiment 21-61

[0047] 1) Use a fixed bed reactor: put 1.0g of catalyst into the reaction tube, keep the pressure in the reactor at 0.1MPa, the temperature at 60°C, and the hydrogen flow rate at 120mL / min. pumped into the reactor. The reaction results are shown in Table 2.

[0048] The influence of table 2 catalyst on the hydrogenation reaction of diacetone alcohol

[0049]

[0050]

[0051] As can be seen from Table 2, different metal catalysts all have certain activity to diacetone alcohol. Among them, Ru / C-CR has the best activity. Therefore, we used Ru / C-CR as the catalyst to investigate the effects of different hydrogen pressures, reaction temperatures, mass space velocities of reaction raw materials and catalysts, and hydrogen flow rates on the hydrogenation reaction in a fixed-bed reactor. The results are shown in Table 3.

[0052] Table 3. Effects of temperature, pressure, mass space velocity, and hydrogen flow rate on the hydrogenation reaction activity of diacetone alcohol ...

Embodiment 62-98

[0060] 3. Dehydration-Diels-Alder reaction: The MPD obtained after the hydrogenation product was purified in the previous step is used as a raw material for this reaction.

[0061] 1) Using a tank reactor: Add 45 g of raw materials and 4.5 g of catalyst into a 100 mL reactor, and stir for 6 h at 170° C. under normal pressure. The detailed reaction results are shown in Table 5.

[0062] Table 5 MPD dehydration-Diels-Alder reaction and its results

[0063]

[0064]

[0065] As can be seen from Table 5, strong acids are more conducive to the reaction, and Nafion and p-toluenesulfonic acid have the best activity. Considering that p-toluenesulfonic acid dissolves in the reaction product water after the reaction, and that p-toluenesulfonic acid itself has great pollution to the environment, we choose the solid acid Nafion as the catalyst and conduct in-depth research on it. Investigate the influence of reaction temperature, reaction pressure, reaction time and catalyst dosag...

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Abstract

The invention relates to a new route for synthesizing liquid naphthenes and aromatics by using lignocellulose-based platform compounds as raw materials through catalytic conversion. The liquid naphthenes and aromatics obtained through this route can be directly used as substitutes for aviation kerosene (or diesel oil) or as additives to improve fuel volume calorific value and sealing performance. The present invention is divided into four parts: 1) Lignocellulose-based platform compound——4-hydroxy-4-methyl-2-pentanone (also known as diacetone alcohol), under the action of a metal catalyst, hydrogenation obtains 2-methanone 2,4-pentanediol (MPD); 2) hydrogenation product——MPD, under the action of an acid catalyst, obtain a cycloolefin compound with a carbon number between 8 and 16 by dehydration and Diels-Alder reaction; 3) Hydrogenate the dehydration-Diels-Alder reaction product to obtain naphthenic compounds for aviation kerosene; 4) The hydrogenation product——MPD, under the joint action of an acid catalyst and a metal catalyst, obtains a carbon number between 8 and 16 aromatic compounds.

Description

technical field [0001] The invention belongs to the field of aviation kerosene, in particular to a method for preparing naphthenes and aromatics for aviation kerosene, and prepares naphthenic compounds and aromatic compounds for aviation kerosene. Background technique [0002] Aviation kerosene, as a liquid fuel in great demand in the world at present, is generally composed of mixed hydrocarbons with carbon numbers between 8 and 16. At present, aviation kerosene is mainly obtained from petroleum refining. However, due to the non-renewability of fossil resources and people's increasing concern for environmental issues, it has become a research hotspot all over the world to find renewable organic carbon sources to replace petroleum to prepare aviation kerosene. Compared with fossil energy, biomass fuel is renewable and carbon dioxide neutral. The sulfur dioxide emitted by bio-jet fuel during combustion is also much lower than that of fossil fuel. Therefore, the research and ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10G3/00
CPCY02P30/20
Inventor 李宁陈芳张涛李广亿王爱琴王晓东丛昱
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI