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Method for preparing cyclohexane through benzene hydrogenation by synergistic catalysis of normal pressure plasma

A normal-pressure plasma and plasma technology are applied in the field of ion-co-catalyzed hydrogenation of benzene to prepare cyclohexane, can solve problems such as undiscovered, and achieve the effects of reducing energy consumption, simple operation process and mild reaction conditions

Inactive Publication Date: 2013-08-21
ZHENGZHOU UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Hydrogenation reaction is a large class of reactions in chemistry. The hydrogenation reaction of benzene under the plasma environment is studied. At present, the hydrogenation of benzene under the synergistic effect of plasma and catalysis has not been reported in the relevant literature at home and abroad. No matter from scientific research or Practical applications have a certain value

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  • Method for preparing cyclohexane through benzene hydrogenation by synergistic catalysis of normal pressure plasma

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] Embodiment 1: a kind of method of atmospheric pressure plasma synergistic catalytic benzene hydrogenation to prepare cyclohexane

[0037] The method for preparing cyclohexane through the synergistic catalysis of benzene hydrogenation by atmospheric pressure plasma of the present invention, the detailed steps of the preparation method are as follows:

[0038] a. Preparation of metal oxide catalyst: Weigh nickel nitrate Ni (NO 3 ) 2 , adding water to make a molar concentration of 0.5 mol·L -1 The solution, according to the ratio between the diatomite and the prepared nickel nitrate solution is 1g: 10ml, take by weighing the catalyst carrier diatomite, dipping the diatomite into the prepared nickel nitrate solution, dipping 10h, take out after the dipping Drying (drying temperature is 100°C, drying time is 6h), after drying, it is placed in a muffle furnace for roasting, roasting temperature is 500°C, roasting time is 4h, and metal oxide catalyst is obtained after roasti...

Embodiment 2

[0044] Embodiment 2: It is basically the same as Embodiment 1, except that:

[0045] In step a: take by weighing nickel nitrate Ni (NO 3 ) 2 , adding water to make a molar concentration of 0.6 mol L -1 solution, the ratio between diatomite and the prepared nickel nitrate solution is 1g:8ml, the dipping time is 14h, after dipping, take out and dry (drying temperature is 120 ° C, drying time is 5h), roasting temperature The calcination time was 650°C, the calcination time was 2h, and the calcined metal oxide catalyst was placed in hydrogen plasma and reduced for 45min;

[0046] In step b: the mass ratio between the metal oxide catalyst and the glass fiber is 1:1;

[0047] In step c: the ratio of the amount added between the metal oxide catalyst and the volume of the plasma reactor is 0.2 g: 24 mL, and argon gas with a flow rate of 40 mL / min is passed through at a constant temperature of 25 ° C and the saturated vapor pressure is reached. Put it into a thermostatic bottle wit...

Embodiment 3

[0050] Embodiment 3: It is basically the same as Embodiment 1, except that:

[0051] In step a: take by weighing nickel nitrate Ni (NO 3 ) 2 , adding water to make a molar concentration of 0.3 mol L -1 The ratio between diatomite and the prepared nickel nitrate solution is 1g:12ml, and the immersion time is 9h. After immersion, it is taken out for drying (drying temperature is 100 °C, drying time is 6.5h), and roasting The temperature is 450°C, the calcination time is 5h, and the calcined metal oxide catalyst is placed in hydrogen plasma and reduced for 50min;

[0052] In step b: the mass ratio between the metal oxide catalyst and the glass fiber is 5:1;

[0053] In step c: the ratio of the amount added between the metal oxide catalyst and the volume of the plasma reactor is 0.5 g: 24 mL, and argon gas with a flow rate of 40 mL / min is passed through at a constant temperature of 15°C and the saturated vapor pressure is reached. Put it into a thermostatic bottle with liquid ...

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Abstract

The invention discloses a method for preparing cyclohexane by synergistically catalyzing the hydrogenation of benzene with atmospheric pressure plasma. First, nickel nitrate or copper nitrate is weighed to prepare a solution, and then the carrier diatomite is dipped into the nickel nitrate solution or copper nitrate solution. , take out and dry after impregnating, roast after drying, obtain metal oxide catalyst after roasting, place the obtained metal oxide catalyst in hydrogen plasma for reduction; In the reactor, the raw material gas is passed into the plasma reactor for catalytic reaction, and the resulting gas product is analyzed after the reaction. Through the technical scheme of the invention, cyclohexane can be prepared by hydrogenating benzene at normal temperature and pressure, the process is simple, the reaction conditions are mild, and energy consumption is greatly reduced. Moreover, the conversion rate of raw materials can reach more than 90%, and the selectivity of cyclohexane is higher, and its selectivity can reach more than 75%.

Description

technical field [0001] The invention relates to a method for preparing cyclohexane, in particular to a method for preparing cyclohexane by synergistically catalyzing the hydrogenation of benzene with atmospheric pressure plasma. Background technique [0002] Benzene hydrogenation reaction is an important hydrogenation reaction, which is mainly used to prepare cyclohexane, a commonly used chemical intermediate. Cyclohexane is mainly used in the preparation of cyclohexanol and cyclohexanone, and is also used in the synthesis of nylon 6. Cyclohexane is widely used as a solvent in the paint industry and is an excellent solvent for resins, fats, paraffin oils, butyl rubber, etc. [0003] At present, there are two main methods of hydrogenation of benzene to prepare cyclohexane: gas-phase method and liquid-phase method. [0004] 1. Method for preparing cyclohexane by gas-phase benzene hydrogenation: [0005] The commonly used gas phase methods are Brxane method, ARCO method, UOP...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C13/18C07C5/10B01J23/755
CPCY02P20/52
Inventor 周彩荣杨勇高石晓华王海峰蒋登高于欣詹自力
Owner ZHENGZHOU UNIV