Unlock instant, AI-driven research and patent intelligence for your innovation.

The method of improving the selective oxidation hydrogen removal rate of co mixed gas

A mixed gas, selective oxidation technology, applied in chemical instruments and methods, carbon monoxide, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problems of high CO loss rate and low hydrogen removal rate, and achieve good The effect of technical effects

Active Publication Date: 2014-10-15
CHINA PETROLEUM & CHEM CORP +1
View PDF4 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The technical problem to be solved by the present invention is that there are high CO loss rate and low hydrogen removal rate in the process of selective oxidation and hydrogen removal in the presence of carbon monoxide in the prior art, and a new method for improving the selective oxidation hydrogen removal rate of CO mixed gas Methods

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0018] Catalyst preparation:

[0019] Weigh 100 grams of alumina carrier, according to 0.5% Pd / Al 2 o 3 The content of the catalyst is configured as follows: select palladium nitrate, prepare an impregnation solution according to the palladium load, immerse the alumina carrier in the solution for 10 hours, and dry it in vacuum at room temperature for 12 hours to obtain a solid. The solid was then dried at 120°C for 4 hours and calcined at 450°C for 6 hours to obtain the required 0.5% Pd / Al 2 o 3 (Active components are in weight percent, the same below) Catalyst.

[0020] Weigh the required amount of catalyst and load it into a fixed-bed reactor, and then use a mixed gas of oxygen and nitrogen with an oxygen volume content of 10% as the processing gas at a temperature of 200 ° C and a volume space velocity of 3000 hours -1 , under the condition of a pressure of 0.5 MPa, the CO mixed gas is selectively oxidized and dehydrogenated by the catalyst for 3 hours, and then the CO ...

Embodiment 2

[0022] Prepare 0.4%Pd / Al according to the catalyst preparation method of embodiment 1 2 o 3 catalyst.

[0023] Weigh the required amount of catalyst and load it into a fixed-bed reactor, and then use a mixed gas of oxygen and nitrogen with an oxygen volume content of 10% as the processing gas, at a temperature of 120°C and a volume space velocity of 5000 hours -1 , under the condition of pressure of 1.5MPa, the CO mixed gas is treated with the catalyst for selective oxidation and hydrogen removal for 8 hours, and then the CO mixed gas is directly fed into the raw material gas for selective oxidation and hydrogen removal for reaction, and the hydrogen in the reaction effluent is oxidized to water. Among them, the CO mixed gas selectively oxidizes the raw material gas to remove hydrogen, the volume percentage of hydrogen is 8%, the reaction temperature is 200°C, and the volume space velocity is 2000 hours -1 , the reaction pressure is 0.5MPa, the molar ratio of hydrogen in the...

Embodiment 3

[0025] Prepare 0.2%Pd / Al according to the catalyst preparation method of embodiment 1 2 o 3 catalyst.

[0026] Weigh the required amount of catalyst and load it into a fixed-bed reactor, and then use a mixed gas of oxygen and nitrogen with an oxygen volume content of 50% as the processing gas at a temperature of 250°C and a volume space velocity of 8000 hours -1 , under the condition of 0.1MPa pressure, the CO mixed gas is treated with the catalyst for selective oxidation and hydrogen removal for 1 hour, and then the CO mixed gas is directly fed into the raw material gas for selective oxidation and hydrogen removal for reaction, and the hydrogen in the reaction effluent is oxidized to water. Among them, the CO mixed gas selectively oxidizes the raw material gas to remove hydrogen, the volume percentage of hydrogen is 6%, the reaction temperature is 260°C, and the volume space velocity is 6000 hours -1 , the reaction pressure is 1.0MPa, the mol ratio of hydrogen in the oxygen...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

No PUM Login to View More

Abstract

The invention relates to a method for improving the selective oxidation dehydrogenation rate of CO mixed gas and mainly solves the technical problems of low hydrogen desorbing rate and high loss rate of CO in the prior art. In the invention, by adopting oxygen with the oxygen volume content of 5 to 100 percent, and mixed gas of at least one inert gas in nitrogen, methane, helium or argon gas, as treatment gases, and under the conditions that the temperature ranges from 100 to 300 DEG C, the volume space velocity is 100 to 10,000 hours<-1>, and the pressure is 0 to 3.0 MPa, the invention adopts technical scheme that 0.5 to 10 hours of treatment is performed on a catalyst for selective oxidation dehydrogenation of CO mixed gas, then the CO mixed gas is led in directly, the gas is enabled to be in contact with the catalyst for selective oxidation dehydrogenation, and hydrogen in effluent produced after reaction is oxidized into water. Therefore, the problems are well solved, and the method can be used in industrial production of oxidation dehydrogenation of the CO mixed gas.

Description

technical field [0001] The invention relates to a method for improving the selective oxidation hydrogen removal rate of CO mixed gas, in particular to a method for improving the oxidation hydrogen removal rate of CO coupling oxalate raw material gas. Background technique [0002] Oxalate is an important organic chemical raw material, which is widely used in the fine chemical industry to produce various dyes, medicines, important solvents, extractants and various intermediates. In the 21st century, oxalate, as a degradable and environmentally friendly engineering plastic monomer, has received extensive international attention. In addition, oxalic acid can be obtained by normal pressure hydrolysis of oxalate, and oxalamide can be obtained by normal pressure ammonia solution. Oxalate can also be used as a solvent to produce pharmaceutical and dye intermediates, etc., such as various condensation reactions with fatty acid esters, cyclohexylacetophenone, amino alcohols, and many...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Patents(China)
IPC IPC(8): C01B31/18B01J23/44B01J23/89C01B32/40
Inventor 杨为民刘俊涛王万民李蕾
Owner CHINA PETROLEUM & CHEM CORP