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Preparation method of perhydrofluorene or perhydrofluorene alkyl substitute

一种氢芴烷基、取代物的技术,应用在高能量密度燃料合成领域,能够解决衍生物条件苛刻、成本高、卤素分离回收困难等问题,达到原料来源绿色、易规模化生产、操作流程复杂的效果

Active Publication Date: 2016-07-06
TIANJIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among them, there are two sources of fluorene: one is coal tar, and fluorene contains about 1.0-2.0% in high-temperature tar. After cooling, crystallization, and centrifugation, crude fluorene is obtained, and then industrial fluorene is dissolved in benzene, and then neutralized Washing with water, solvent removal, re-distilling fluorene, and recrystallizing the distillate with gasoline and ethanol to obtain 95% pure fluorene. This method consumes a lot of energy; the second is to generate intramolecular or Intermolecular alkylation, for example, Angewandte Chemie International Edition 2012, 51 (22), 5359-5362 uses Ru to activate the C-H of 2,2-diphenylacetic acid, and cyclizes to obtain fluorene; Angewandte Chemie International Edition 2010, 49 (16), 2909-2912 Using Ru to catalyze the cross-coupling and intramolecular cyclization of 1,2-dihalobenzene and phenylboronic acid to obtain fluorene; , 1'-biphenyl undergoes an intramolecular alkylation reaction to obtain fluorene, but this method is expensive and difficult to realize industrialization
One method of mass production of fluorene is the alkylation reaction of dichloromethane and benzene or biphenyl under the catalysis of aluminum trichloride, but this method introduces toxic benzene, and the introduced halogen is separated and recovered Difficult, high production cost, heavy environmental pollution, and the conditions for reducing fluorene derivatives are harsh and the yield is low

Method used

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  • Preparation method of perhydrofluorene or perhydrofluorene alkyl substitute
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  • Preparation method of perhydrofluorene or perhydrofluorene alkyl substitute

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0027] Add 25.2g of anisole, 3.08g of dibenzyl ether, and 0.1g of MMT-K10 into a three-necked flask with a volume of 50mL, stir magnetically, and react at a temperature of 110°C for 2 hours; transfer the above reaction mixture to a distillation apparatus for decompression Purified by distillation, and collected fractions at a temperature of 160-210°C at -0.08 MPa to obtain 6 g of colorless organic fractions.

[0028] Use gas chromatography to analyze the alkylation reaction product of preparing diphenylmethane derivatives, dibenzyl ether conversion rate 100%, anisole conversion rate 15%, diphenylmethane derivatives (i.e. substituted or unsubstituted diphenylmethane ) Yield 90%. After distillation under reduced pressure, pure diphenylmethane or a mixture of diphenylmethane with substituents can be obtained.

Embodiment 2-18

[0030] Same as embodiment 1, SiO 2 -Al 2 o 3 , HZSM-5, Al-MCM-41, Hβ, MMT-K10, SAPO-34, USY, H 3 o 40 PW 12· wxya 2 O(HPW), Amberlyst-15, Nafion, AlCl 3 , FeCl 3 , ZnCl 2 , CuCl 2 , metal-modified HPW (such as Sn 0.5 TPA, HfTPA), Nb 2 o 5 、WO 3 Such metal oxides and liquid phosphoric acid can respectively catalyze lignin containing benzene ring derivatives and benzyl compounds (2-methylbenzyl alcohol, 4-methylbenzyl alcohol, isomers of 2-methylbenzyl alcohol, benzene Alkylation reaction of methanol and benzyl alcohol dehydration condensation product (dibenzyl ether, etc.). Now the results of the yield of catalyst and its consumption, reactant conversion rate, reactant ratio, temperature of reaction, reaction time, and diphenylmethane derivative (i.e. substituted or unsubstituted diphenylmethane) are listed in Table 1:

[0031] Table 1

[0032]

[0033]

[0034] It can be seen from the above Examples 1-18 that lignin derivatives (phenols or aromatic hydroca...

Embodiment 19

[0036] Adding 30g o-benzyl anisole, 3.6g palladium carbon, and 3gHZSM-5 catalyst into a 100mL pressure reactor with stirring, wherein the mass percentage of palladium in the palladium carbon is 5wt%, and the stirring rate is 680 rev / min, under the conditions of hydrogen pressure of 6 MPa and temperature of 200° C. for 10 hours, and centrifugation to obtain 26 g of colorless organic liquid.

[0037] The prepared fuel was analyzed by GC-MS analysis and the product was composed of two components (including a mixture of 35% dicyclohexylmethane and 65% perhydrofluorene in yield).

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Abstract

The invention discloses a preparation method of a perhydrofluorene or perhydrofluorene alkyl substitute.The preparation method includes following steps: (1), enabling a phenol compound or an aromatic hydrocarbon compound or an arone compound or an aromatic ether compound to be in alkylation reaction with a benzyl compound in the presence of a first catalyst to generate substituted or unsubstituted diphenylmethane, wherein the first catalyst is an acidic catalyst; (2), enabling the substituted or unsubstituted diphenylmethane to be in hydrogenation or hydrogenation and dehydrogenation reaction with hydrogen in the presence of a second catalyst to obtain the perhydrofluorene or perhydrofluorene alkyl substitute, wherein the second catalyst is a mechanical mixture of a metal catalyst and an acid catalyst or the metal catalyst loaded on the acid catalyst.

Description

technical field [0001] The invention belongs to the field of high energy density fuel synthesis and relates to a preparation method of perhydrofluorene or perhydrofluorene alkyl substitutes. Background technique [0002] High-density fuel is a synthetic liquid hydrocarbon used as fuel. In essence, it is the same as hydrocarbon fuel refined from petroleum, such as aviation kerosene JetA, rocket kerosene RP-1, etc., and can be applied to all kerosene-based fuels. Fuel for air-breathing engines and rocket engines. Compared with petroleum refining fuels, the density of high-density fuels has been greatly improved, and the mass combustion calorific value is basically the same, so it can also be called high energy density fuels, and its volume calorific value has been greatly improved. Under the condition of a certain volume of the fuel tank, more propulsion power can be provided, and the range or carrying capacity of the aircraft can be significantly improved. [0003] High-den...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C13/567C07C1/20C07C5/00
CPCC07C1/20C07C5/00C07C37/00C07C41/18C07C13/567C07C39/15C07C43/23C07C43/205C07C43/2055C07C15/16C07C37/16C07C41/30C07C1/22C07C45/70C07C5/13C07C2521/18C07C2523/06C07C2523/20C07C2523/28C07C2523/30C07C2523/42C07C2523/44C07C2523/46C07C2523/72C07C2523/745C07C2523/75C07C2523/755C07C2523/882C07C2523/89C07C2527/122C07C2527/126C07C2527/128C07C2527/138C07C2527/173C07C2527/188C07C2529/08C07C2529/40C07C2529/70C07C2529/85C07C2531/10C07C2603/18C10L1/04C07C2/864C07C2/865C07C15/50C07C49/784C07C2603/10C07C29/32C07C45/61
Inventor 邹吉军潘伦张香文王庆法王莅
Owner TIANJIN UNIV
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