Preparation and application methods for non-noble metal catalyst used for liquid-phase reaction system used in acetylene hydrogenation

A liquid-phase reaction, acetylene hydrogenation technology, applied in metal/metal oxide/metal hydroxide catalysts, catalysts, hydrogenation to hydrocarbons, etc. The problem of high cost, to achieve the effect of excellent catalytic ability, easy control, simple and fast operation

Pending Publication Date: 2017-07-21
SHENWU TECH GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

None of the previous studies involved the solvothermal stability of the catalyst dispersed in the liquid solvent, but in the new reaction system, the solvothermal stability of the catalyst has a great impact on the life of the catalyst as well as the catalytic activity and selectivity, so it must be highly valued , unfortunately no related reports have been seen
At the same time, acetylene produced by calcium carbide method and purified may still contain H 2 S, AsH 3 、PH 3 Such impurity gases can easily lead to catalyst poisoning. The anti-poisoning ability of the catalyst in the liquid phase also needs to be investigated, and the regeneration of the catalyst is difficult.
At the same time, the traditional catalytic hydrogenation uses the noble metal Pd as the main active component, and Ag, Au and other additives need to be added, and the cost of the catalyst is relatively high. However, although the research on the performance of Ni in selective catalytic hydrogenation has decreased, due to its preparation Still gaining traction at a lower cost

Method used

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  • Preparation and application methods for non-noble metal catalyst used for liquid-phase reaction system used in acetylene hydrogenation

Examples

Experimental program
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Effect test

Embodiment 1

[0030] A method for preparing a non-noble metal catalyst for acetylene hydrogenation liquid phase reaction system, comprising the steps of:

[0031] In the step (1) shown in box S100, weigh 6g of nickel nitrate and 20g of zinc nitrate and dissolve them in 30g of deionized water, add 1g of hexamethylenetetramine and 1g of PVP at the same time and ultrasonicate for 10 minutes at 60°C. Set as 360W, recorded as solution I;

[0032] In step (2) shown in frame S200, take the α-Al of 100g 2 o 3 Add it to 60g of NMP, mix it with the above solution I, and transfer it to a static kettle, place it in an ultrasonic container, use an oil bath, set the temperature at 120°C, and control the ultrasonic power at 360W, and control the time for 2 hours;

[0033] In the step (3) shown in block S300, keep the ultrasound turned on and naturally cool to room temperature, centrifuge the mixed solution, take the solid matter, wash it with absolute ethanol for 2 to 3 times, filter it with suction, dr...

Embodiment 2

[0038] A method for preparing a non-noble metal catalyst for acetylene hydrogenation liquid phase reaction system, comprising the steps of:

[0039] Step (1) shown in block S100 is the same as embodiment 1;

[0040] In the step (2) shown in block S200, the temperature of the oil bath is set to 140°C, the power is increased to 420W, and the time is controlled for 3 hours, and the rest are the same as in Example 1;

[0041] Step (3) shown in block S300 and the application method of the non-noble metal catalyst used in the acetylene hydrogenation liquid phase reaction system are the same as in Example 1.

Embodiment 3

[0043] A method for preparing a non-noble metal catalyst for acetylene hydrogenation liquid phase reaction system, comprising the steps of:

[0044] In step (1) shown in box S100, add 4g hexamethylenetetramine and 2g PVP, all the other are the same as embodiment 1;

[0045] In the step (2) shown in block S200, the power is increased to 960W, the oil bath is 120°C, and the time is controlled for 4 hours, and the rest are the same as in Example 1;

[0046] Step (3) shown in block S300 is the same as that in Embodiment 1.

[0047] A method for applying a non-precious metal catalyst in a liquid-phase reaction system for hydrogenation of acetylene, comprising the following steps:

[0048] Step 1) is the same as embodiment 1;

[0049] Step 2) Put the obtained catalyst and nitrogen-methylpyrrolidone (NMP) into a reactor to form a solution, hydrogen and acetylene form a raw material gas with a molar ratio of 5:1, and react continuously at 145°C, and the rest of the conditions are th...

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Abstract

The invention discloses preparation and application methods for a non-noble metal catalyst used for a liquid-phase reaction system used in acetylene hydrogenation. According to the invention, a liquid-phase substance in a gas-liquid-solid reaction system is used as a solvent for catalyst synthesis, a metal nitrate is used as a metal ion source, a solvent-thermal synthesis method is employed, and a series of synthesis conditions are regulated so as to eventually prepare the ideal catalyst; meanwhile, before introduction of acetylene gas into the catalyst, the catalyst is subjected to low-temperature reduction in an alkaline liquid-phase environment under the action of reducing agents like sodium borohydride. In evaluation and application of the catalyst, reaction gas comes from carbide acetylene gas and is accompanied by impurity gases like H2S, AsH3 and PH3. The catalyst prepared in the invention has a cheap price, high catalytic activity, good selectivity, strong anti-poisoning capability and solvothermal resistance and is of great significance to industrial promotion of preparation of ethylene via a carbide acetylene method.

Description

technical field [0001] The invention relates to the technical field of ethylene preparation in coal chemical industry, in particular to a preparation and application method of a non-noble metal catalyst used in an acetylene hydrogenation liquid phase reaction system. Background technique [0002] In the field of petrochemical industry, the process of preparing ethylene from petroleum cracking usually contains a small amount of acetylene. In order to prevent acetylene from poisoning the ethylene polymerization catalyst, it is necessary to remove acetylene in the industry, and the catalytic selective hydrogenation of acetylene is the most effective one. method is also a research hotspot in recent years. The reaction system of the catalyst is also aimed at reducing the process conditions of hydrogenation of acetylene to ethylene in an ethylene-rich environment. In the coal chemical technology, the production of acetylene by using coal as raw material through the calcium carbid...

Claims

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Application Information

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IPC IPC(8): B01J23/80C07C5/09C07C11/04
CPCY02P20/52B01J23/80C07C5/09C07C2523/80C07C11/04
Inventor 史东军史雪君刘周恩余海鹏吴黎阳黄伟苏二强吴道洪
Owner SHENWU TECH GRP CO LTD
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