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Method of preparing cyclopentane by continuous hydrogenation of cyclo pentadiene

A technology for cyclopentadiene and cyclopentane production, which is applied in the directions of hydrogenation to hydrocarbon production, organic chemistry, etc., can solve the problems of catalyst deactivation, reduction of cyclopentane yield, limitation of cooling uniformity, etc., and improves the reaction yield , The effect of easy reaction and uniform temperature

Inactive Publication Date: 2007-02-14
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The method of installing a heat exchange device in the hydrogenation reactor is used to remove the reaction heat generated during the hydrogenation of cyclopentadiene. The disadvantage is that the uniformity of cooling in the reactor is limited to a certain extent.
It is speculated that there is still a local excessive temperature rise in the catalyst bed, which causes partial catalyst deactivation, and cyclopentadiene is easily dimerized to form dicyclopentadiene in this high-temperature region, which will reduce the concentration of cyclopentane. yield

Method used

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  • Method of preparing cyclopentane by continuous hydrogenation of cyclo pentadiene
  • Method of preparing cyclopentane by continuous hydrogenation of cyclo pentadiene
  • Method of preparing cyclopentane by continuous hydrogenation of cyclo pentadiene

Examples

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Effect test

Embodiment 1~8

[0021] The process flow of each embodiment of the present invention is shown in the accompanying drawings. The reactor 1 is a fixed-bed reactor, and a Venturi injector 2 is arranged on the top of the reactor. The raw material cyclopentadiene M1, the solvent M2 and the externally circulated reaction liquid M4 enter the raw material blending tank for mixing. The liquid phase material from the raw material preparation tank and the raw material hydrogen M3 are fully mixed and atomized in the Venturi injector 2 to form a mist-like gas-liquid mixture, and then pass through the fixed-bed catalyst bed for hydrogenation reaction. The reaction liquid from the reactor enters the reaction liquid storage tank 4, and then passes through the external circulation heat exchanger for heat exchange and cooling. The cooled reaction solution is divided into two parts, one is the external circulation part M4, the other is the discharge M5, M4 returns to the raw material preparation tank 3, and M5 e...

Embodiment 9

[0024] Except that the solvent adopts tert-butanol, all the others are the same as in Examples 1-8, and other process conditions are listed in Table 1.

Embodiment 10

[0026] Except that the solvent adopts n-hexane, all the others are the same as in Examples 1-8, and other process conditions are listed in Table 1.

[0027] The reaction results of each embodiment are shown in Table 2.

[0028] CPD / solvent

(weight ratio)

CPD / H 2

(mol ratio)

reaction pressure

(MPa)

temperature reflex

(℃)

Catalyst load

(hr -1 )

M5 / M4

(weight ratio)

Example 1

1∶8

1∶3.3

1.5

64

2.5

1∶8

Example 2

1∶8

1∶3.1

1.2

62

2.5

1∶8

Example 3

1∶8

1∶3.1

0.9

60

2.5

1∶8

Example 4

1∶8

1∶4.0

1.8

72

2.5

1∶10

Example 5

1∶5

1∶3.3

1.5

55

2.5

1∶12

Example 6

1∶10

1∶3.0

1.8

44

2.0

1∶9

Example 7

1∶10

1∶3.0

1.5

50

2....

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Abstract

The continuous cyclopentadiene hydrogenating process to prepare cyclopentane is one continuous catalytic hydrogenation reaction of the mixture of cyclopentadiene, solvent and hydrogen in a fixed bed catalyst bed. The catalyst includes gamma-Al2O3 as carrier and Pa as active component. The solvent is any one of cyclopentane, n-hexane, benzene, toluene, cyclohexane, ethanol, methanol, etc. The molar ratio between cyclopentadiene and hydrogen is 1 to (3-4), and the reaction system has pressure of 0.9-1.8MPa and temperature of 44-72 deg.c. The reacted liquid is discharged partially and externally circulated partially with the weight ratio being 1 to 6-12, and the externally circulated liquid after being cooled is mixed with cyclopentadiene material and solvent before being mixed with hydrogen in venturi ejector, atomized into gas-liquid mixture and reacted in the catalyst bed. The catalyst load is 2-4 / hr accounted in liquid phase material, and the reacted heat is transferred via external circulation.

Description

technical field [0001] The invention relates to a method for preparing cyclopentane by hydrogenating cyclopentadiene. Background technique [0002] Cyclopentane is a new type of foaming agent that has no side effects on the atmospheric ozone layer. It has been widely used in polyurethane foam materials, especially as a foaming agent for refrigerator insulation materials. In the prior art, cyclopentane can be obtained by various methods, but the method of hydrogenation of cyclopentadiene has the most industrial application prospect. However, since the hydrogenation reaction of cyclopentadiene is a strong exothermic reaction, the catalyst bed is prone to overheating during the catalytic hydrogenation process, resulting in catalyst deactivation. method to remove the large amount of reaction heat generated. For example, Chinese patent ZL00107230.7 provides a method for producing cyclopentane by continuous depolymerization and hydrogenation of dicyclopentadiene. The hydrogenati...

Claims

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Application Information

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IPC IPC(8): C07C13/10C07C5/03
Inventor 郭世卓周飞范存良顾超然
Owner CHINA PETROLEUM & CHEM CORP
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