Nickel-containing catalyst and method for removing H2 in CO raw material

A nickel catalyst and catalyst technology, applied in chemical instruments and methods, physical/chemical process catalysts, carbon monoxide, etc., can solve the problem of high hydrogen content, reduce production costs, avoid explosion risks, and improve production efficiency.

Inactive Publication Date: 2015-03-18
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the method can use non-noble metals as catalysts, the -1 , the H in the obtained reaction tail gas 2 The lowest content is 391ppm, and the content of hydrogen in the tail gas obtained from the reaction is still relatively high, which needs further purification

Method used

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  • Nickel-containing catalyst and method for removing H2 in CO raw material
  • Nickel-containing catalyst and method for removing H2 in CO raw material
  • Nickel-containing catalyst and method for removing H2 in CO raw material

Examples

Experimental program
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Effect test

Embodiment 1

[0048] (1) Preparation of magnetic particles

[0049] 189g Na 2 SiO 3 9H 2 O was dissolved in 1000 mL of distilled water, and 3 mol / L HCl solution was slowly added dropwise under stirring condition to adjust the pH value of the solution to 13, and filtered for later use.

[0050] Add 42.2 g of FeCl to a 3 L stirred tank with 1200 mL of distilled water 3 ·6H 2 O and 20.6gFeCl 2 4H 2 O, heat up to 85°C, add 60mL of 25% NH during high-speed stirring 3 ·H 2 O solution, after stirring at high speed for 3 minutes, use a magnetic separator to separate the black Fe 3 o 4 Particles (particle size 3-30nm). The cleaned black Fe 3 o 4 Particles were ultrasonically dispersed in the above pretreated Na 2 SiO 3 solution, then moved it into a 3L stirred tank, raised the temperature to 85°C, and added dropwise HCl solution with a concentration of 2mol / L to the solution under the condition of nitrogen protection and stirring, within 3 hours, the pH value of the solution was reduce...

Embodiment 2

[0060] (1) Preparation of magnetic particles

[0061] 28.4g Na 2 SiO 3 9H 2 O was dissolved in 600 mL of distilled water, and 3 mol / L HCl solution was slowly added dropwise under stirring condition to adjust the pH value of the solution to 13, and it was filtered for later use.

[0062] Add 46.7 g of FeCl to a 2 L stirred tank with 1000 mL of distilled water 3 ·6H 2 O and 17.2 g FeCl 2 4H 2 O, heat up to 90°C, add 160mL of 6mol / L NaOH solution during high-speed stirring, and after 3 minutes of high-speed stirring, use a magnetic separator to separate the black Fe 3 o 4 Particles (particle size 3-30nm). The cleaned black Fe 3 o 4 Particles were ultrasonically dispersed in the above pretreated Na 2 SiO 3 solution, then moved it into a 2L stirred tank, raised the temperature to 90°C, and added dropwise HCl solution with a concentration of 2mol / L to the solution under the condition of nitrogen protection and stirring, within 3 hours, the pH value of the solution was re...

Embodiment 3

[0072] (1) Preparation of magnetic particles

[0073] 189g Na 2 SiO 3 9H 2 O was dissolved in 1000 mL of distilled water, and 3 mol / L HCl solution was slowly added dropwise under stirring condition to adjust the pH value of the solution to 13, and filtered for later use.

[0074] Ultrasonic dispersion of 14.54g of black iron powder (particle size 3-30nm) particles in the above pretreated Na 2 SiO 3 solution, and then moved into a 3L stirred tank, heated to 95°C, under nitrogen protection and stirring conditions, added dropwise HCl solution with a concentration of 2mol / L to the solution, within 3 hours, the pH value of the solution was reduced from 13 to 6. Filter to get 60g white SiO 2 Magnetic particles coated with iron powder particles (wherein, the iron powder weighs about 20g, and the SiO coated on the surface of the iron powder particles 2 About 40g, the weight ratio of silicon dioxide to iron powder is 2:1). The magnetic hysteresis loop detected by the vibrating s...

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Abstract

The invention provides a nickel-containing catalyst. The nickel-containing catalyst contains a magnetic carrier and nickel which accounts for 5-30 weight percent of the nickel-containing catalyst and is loaded on the magnetic carrier. The invention further provides a method for removing H2 in a CO raw material. The method comprises the following steps: making the CO raw material be contact with the nickel-containing catalyst under the condition of a methanation reaction, wherein the nickel-containing catalyst is the nickel-containing catalyst provided by the invention. The method for removing H2 in the CO raw material, provided by the invention, can be used for rapidly reducing the content of H2 in the CO raw material to below 310ppm by adopting the nickel-containing catalyst without adopting a precious metal catalyst or adding oxygen in the reaction.

Description

technical field [0001] The invention relates to a nickel-containing catalyst, and the use of the nickel-containing catalyst to remove H in CO raw materials 2 Methods. Background technique [0002] The technology of using coal or natural gas instead of petroleum ethylene to synthesize ethylene glycol through oxalate is recognized as the most scientific raw material route, the most reasonable resource utilization, and obviously superior to the petroleum route. According to calculations, if the world’s 22 million tons of ethylene glycol produced from petroleum ethylene are produced with this technology, it is equivalent to the successful development of a new Daqing Oilfield with an annual output of 55 million tons of oil above the scale, and its output value is nearly 200 billion yuan. . Combined with my country's current situation of lack of oil, gas, and relatively rich coal resources, the development of technology for preparing ethylene glycol from coal has significant eco...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/83B01J23/755C01B31/18C01B32/40
Inventor 潘智勇慕旭宏宗保宁
Owner CHINA PETROLEUM & CHEM CORP
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