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Method of selective oxidation of hydrogen in propane dehydrogenation process

A propane dehydrogenation, selective technology, applied in chemical instruments and methods, physical/chemical process catalysts, hydrocarbons, etc., can solve the problems of low oxygen conversion rate and high hydrocarbon consumption

Active Publication Date: 2015-02-11
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The technical problem to be solved by the present invention is that there are problems in the prior art that the oxygen conversion rate is relatively low and the consumption of hydrocarbons is high, and a new method for selective oxidation of hydrogen in the process of propane dehydrogenation is provided

Method used

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  • Method of selective oxidation of hydrogen in propane dehydrogenation process
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  • Method of selective oxidation of hydrogen in propane dehydrogenation process

Examples

Experimental program
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Embodiment 1

[0026] Al 2 o 3 See the patent (patent application number: 201010146868.4) for the preparation of the carrier, the same below.

[0027] Weigh 2 grams of particles with a size of 10 nanometers and a specific surface area of ​​50 meters 2 / g, nano-Al with a pore size of 29 nm 2 o 3 Carrier, add 10 ml of deionized water, respectively pipette 0.18 ml of H with a mass concentration of 0.004 g / ml 2 PtCl 6 solution and 1.44 ml of Ce(NO with a mass concentration of 0.0012 g / ml 3 ) 4 solution, add dropwise 0.022 g of SnCl 4 solution, use 2.5% ammonia water to adjust the pH value of the solution to 3.5, then soak it in a water bath at 80°C for 1 hour, take out the sample and filter it, dry it in an oven at 120°C for 8 hours, and then put the sample into a muffle furnace at 550°C ℃ for 4 hours to obtain the desired catalyst. The prepared catalyst is loaded into a fixed-bed reactor, propane in the feed gas: propylene: hydrogen: the oxygen molar ratio is 1: 1: 0.5: 0.25, at 1 atmo...

Embodiment 2

[0029] Weigh 2 grams of particles with a size of 60 nanometers and a specific surface area of ​​50 meters 2 / g, nano-Al with a pore size of 29 nm 2 o 3 Carrier, add 10 ml of deionized water, respectively pipette 0.88 ml of H with a mass concentration of 0.004 g / ml 2 PtCl 6 solution and 7.2 milliliters of La(NO 3 ) 4 solution, add dropwise 0.0439 g of SnCl 4 Solution, use 2.5% ammonia water to adjust the pH value of the solution to 1, then soak it in a water bath at 80°C for 1 hour, take out the sample and filter it, dry it in an oven at 120°C for 8 hours, then put the sample into a muffle furnace at 550°C ℃ for 4 hours to obtain the desired catalyst. The prepared catalyst is loaded into a fixed bed reactor, propane in the feed gas: propylene: hydrogen: oxygen molar ratio is 1: 0.2: 0.2: 0.1, at 5 atmospheric pressure, 550 ℃ and space velocity 600 hours -1 The activity evaluation was carried out under the following conditions, and the results were as follows: the selecti...

Embodiment 3

[0031] Weigh 2 grams of particles with a size of 60 nanometers and a specific surface area of ​​50 meters 2 / g, nano-Al with a pore size of 29 nm 2 o 3 Carrier, add 10 ml of deionized water, respectively pipette 0.88 ml of H with a mass concentration of 0.004 g / ml 2 PtCl 6 solution and 7.2 ml of Ce(NO with a mass concentration of 0.0012 g / ml 3 ) 4 solution, drop 0.3295 g of Fe(NO 3 ) 3 solution, use 2.5% ammonia water to adjust the pH value of the solution to 3.5, then soak it in a water bath at 80°C for 1 hour, take out the sample and filter it, dry it in an oven at 120°C for 8 hours, and then put the sample into a muffle furnace at 550°C ℃ for 4 hours to obtain the desired catalyst. The prepared catalyst is loaded into a fixed-bed reactor, propane in the feed gas: propylene: hydrogen: oxygen molar ratio is 1: 0.5: 0.5: 0.25, at 10 atmospheric pressure, 550 ℃ and space velocity 600 hours -1 The activity evaluation was carried out under the following conditions, and th...

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Abstract

The present invention relates to a method of selective oxidation of hydrogen in a propane dehydrogenation process, and mainly solves the problems that conventional hydrogen oxidation catalyst is low in oxygen conversion rate and high in hydrocarbon loss rate. According to the present invention, a hydrogen selective oxidation method is used in a propane dehydrogenation process; propane, propylene, hydrogen and oxygen are used as raw materials; and under the conditions that the reaction temperature is 450-550 DEG C, the reaction pressure is 1-10 atm, and the gas space velocity is 100-1200 h<-1>, H2 and O2 are reacted on the catalyst to produce water, wherein the catalyst comprises the following components by weight: 0.1-10% of Pt, Pd, or an oxide thereof, and 0.25-10% of Sn, Zn, or an oxide thereof, 0.1-10% of Ce, La, Zr, or an oxide thereof and 80-99% of nano-alumina. The technical solution solves the problem well, and can be used in industrial production of selective oxidation of hydrogen in propane dehydrogenation.

Description

technical field [0001] The invention relates to a hydrogen selective oxidation method in the propane dehydrogenation process. Background technique [0002] Propylene is an important organic chemical raw material, its consumption is second only to ethylene, with the global demand for propylene increasing, it will increase to 86.0x10 by 2010 6 t, its growth rate exceeds 1 times that of ethylene. At present, the source of propylene mainly comes from ethylene cracking co-production and refinery by-products, and a small part comes from special production processes, such as propane dehydrogenation reaction, butene and ethylene replacement reaction, alcohol-to-olefin reaction, etc., in these specialized production processes Propane catalytic dehydrogenation to propylene technology plays an increasingly important role in the process. In the method, propane is used as a raw material, and the target product propylene is obtained under the action of a dehydrogenation catalyst, and by...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C11/06C07C5/48B01J23/835B01J23/83
CPCY02P20/52
Inventor 吴省吴文海樊志贵缪长喜
Owner CHINA PETROLEUM & CHEM CORP