Method for producing hydrogen peroxide by anthraquinone process

A technology of hydrogen peroxide and anthraquinone method, applied in chemical instruments and methods, peroxide/peroxyhydrate/peroxyacid/superoxide/ozonide, inorganic chemistry, etc., can solve the liquid phase axis diameter Problems such as uneven distribution, low utilization efficiency of the reactor, and large mass transfer resistance of gas-phase hydrogen can be achieved to achieve uniform distribution, increase reactor efficiency, and reduce energy consumption.

Inactive Publication Date: 2008-07-30
CHINA UNIV OF PETROLEUM (BEIJING)
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The existing fixed-bed reactor technology uses a vertical reactor, and hydrogen and working fluid are fed from the top of the fixed-bed reactor. In this feeding method, the gas phase in the reactor is a continuous phase, and the liquid phase is sprayed from the top. Under the action of gravity, the fixed bed falls in a trickle shape, which is called a trickle bed. To participate in the reaction, gas phase hydrogen needs to pass through the liquid phase mass transfer to reach the surface of the catalyst. The mass transfer resistance of gas phase hydrogen is large, which is not conducive to the hydrogenation reaction. At the same time, due to the uneven distribution of the liquid phase axis and radial direction, it will lead to low local utilization efficiency of the reactor, local overhydrogenation of the catalyst bed will lead to agglomeration, and further aggravate the bias flow so that the bed resistance will rise rapidly and the production operation will not be possible.

Method used

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  • Method for producing hydrogen peroxide by anthraquinone process
  • Method for producing hydrogen peroxide by anthraquinone process

Examples

Experimental program
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Effect test

Embodiment 1

[0020] see figure 1 As shown, in this embodiment, a vertical fixed-bed reactor is adopted to carry out the catalytic hydrogenation reaction of anthraquinone, and the reactor is filled with 30ml Raschig annular Pd / Al 2 o 3 Catalyst and anthraquinone working liquid enter from the bottom of reactor 1, and the effective anthraquinone concentration of the working liquid is 130g / L. Hydrogen is also introduced from the lower part of the reactor, and is distributed into the working liquid in the form of bubbles through the hydrogen distributor 11. Control the hydrogenation reaction temperature in the reactor to about 50°C, the reaction pressure to 0.2MPa, and the liquid space velocity to 12h -1 , hydrogen air velocity 120h -1 .

[0021] After the hydrogenation reaction is completed, the hydrogenation working solution is discharged from the top of the reactor, and is transferred to the oxidation equipment (oxidation tower) to continue oxidation, and the oxidation product is separated ...

Embodiment 2

[0033] The fixed bed reactor and the operation process are the same as in Example 1, the hydrogenation reaction temperature is controlled at about 70°C, and the catalyst is spherical Pd / SiO 2 , the diameter is Φ2mm, and other evaluation conditions are the same as in Example 1.

[0034] Using the traditional feeding method, the hydrogen efficiency recorded is 3.58g / L; using the method of the present invention, using the lower feeding method, the hydrogen efficiency recorded is 5.50g / L, compared with the traditional feeding method, the hydrogen efficiency 53% increase.

Embodiment 3

[0036] The fixed-bed reactor and the operation process are the same as in Example 1, the hydrogenation reaction temperature is controlled at 60°C, the operating pressure is 0.4MPa, and the catalyst is Pd / Al 2 o 3 Φ2×5mm strips, other evaluation conditions are the same as in Example 1.

[0037] Using the traditional feeding method, the measured hydrogen effect is 2.55g / L; using the method of the present invention, using the lower feeding method, the recorded hydrogen effect is 5.11g / L, compared with the traditional feeding method, the hydrogen efficiency 100% increase.

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Abstract

The invention provides a process for producing hydrogen peroxide by using an anthraquinone method. The process includes the following steps: hydrogen is added in the anthraquinone to generate anthrahydroquinone which is oxidized to generate the anthraquinone and the hydrogen peroxide. The reaction in which the hydrogen is added in the anthraquinone to generate anthrahydroquinone means that working fluid with the anthraquinone and the hydrogen are led in a fixed bed reactor which is filled with catalyst with the hydrogen so that hydrogenation is generated between the working fluid with the anthraquinone and the hydrogen to generate the anthrahydroquinone under the effect of the catalyst; the obtained hydrogenated working fluid with the anthrahydroquinone is conducted out of an oxidation device, wherein, when the working fluid with the anthrahydroquinone and the hydrogen are conducted in the fixed bed reactor, the working fluid is continuous phase, in which the hydrogen is distributed in the form of bubbles; when the working fluid with the anthrahydroquinone and the hydrogen are conducted in the fixed bed reactor, a feeding inlet is made not higher than a discharging outlet where the hydrogenated liquid is discharged out of the fixed bed reactor. By using the method, utilization efficiency of the catalyst as well as the production capability of the reactor is promoted and bed resistance is reduced.

Description

technical field [0001] The invention relates to a method for producing hydrogen peroxide by an anthraquinone method, in particular to a method for using a fixed-bed reactor to carry out hydrogenation reaction of anthraquinone and further producing hydrogen peroxide. The invention also relates to a device for carrying out the method. Background technique [0002] Hydrogen peroxide (hydrogen peroxide) is an important inorganic chemical raw material. At present, the method for industrially producing hydrogen peroxide is mainly the anthraquinone method. The main process of producing hydrogen peroxide by anthraquinone method is as follows: a certain proportion of anthraquinone working liquid and hydrogen gas are passed into the hydrogenation tower, and a catalyst is installed in the hydrogenation tower. Under the action of the catalyst, the anthraquinone in the working liquid is hydrogenated to form anthracene Hydroquinone, and then the hydrogenated working liquid (hydrogenated ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B15/023
Inventor 张文慧周红军
Owner CHINA UNIV OF PETROLEUM (BEIJING)
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