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Catalyst for propane dehydrogenation to propylene

A propane dehydrogenation and catalyst technology, which is applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, hydrocarbons, etc., can solve the problem of low selectivity of propane dehydrogenation catalysts

Active Publication Date: 2021-10-01
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] One of the technical problems to be solved by the present invention is the low selectivity of propane dehydrogenation catalysts in the prior art, and a propane dehydrogenation catalyst is provided

Method used

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  • Catalyst for propane dehydrogenation to propylene
  • Catalyst for propane dehydrogenation to propylene
  • Catalyst for propane dehydrogenation to propylene

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] Weigh 52.66 grams of chromium nitrate, 2.15 grams of potassium nitrate, and 3.78 grams of sodium titanate, add them to 100 ml of deionized water, and then add 86 grams of them with a specific surface area of ​​117m 2 / g, aluminum oxide carrier with a pore size of 15nm, adjust the pH value of the solution to 3.5 with 2.5% ammonia water, then soak in a water bath at 80°C for 1 hour, take out the sample for filtration, dry it in an oven at 120°C for 8 hours, and then put the sample Put it into a muffle furnace and bake at 550° C. for 4 hours to obtain the desired catalyst.

[0034]Adjust the flow of propane gas through the mass flow meter, enter the preheating zone for preheating, and then enter the reaction zone. The heating section and the reaction section of the reactor are heated by electric heating wires to make them reach the predetermined temperature. The inner diameter of the reactor is Ф6mm Quartz tube, about 400mm long. After the reaction gas passes through the ...

Embodiment 2

[0037] Weigh 52.66 grams of chromium nitrate, 2.15 grams of potassium nitrate, and 3.78 grams of sodium titanate, add them to 100 ml of deionized water, and then add 86 grams of them with a specific surface area of ​​340m 2 / g, alumina carrier with a pore size of 9nm, adjust the pH value of the solution to 3.5 with 2.5% ammonia water, and then soak it in a water bath at 80°C for 1 hour, take out the sample for filtration, dry it in an oven at 120°C for 8 hours, and then put the sample Put it into a muffle furnace and bake at 550° C. for 4 hours to obtain the desired catalyst. The propane raw material and the above-mentioned catalyst were reacted under the same conditions as in Example 1, and the results are shown in Table 1.

Embodiment 3

[0039] Weigh 52.66 grams of chromium nitrate, 2.15 grams of potassium nitrate, and 3.78 grams of sodium titanate, add them to 100 ml of deionized water, and then add 86 grams of them with a specific surface area of ​​173m 2 / g, aluminum oxide carrier with a pore size of 12nm, adjust the pH value of the solution to 3.5 with 2.5% ammonia water, then soak in a water bath at 80°C for 1 hour, take out the sample for filtration, dry it in an oven at 120°C for 8 hours, and then put the sample Put it into a muffle furnace and bake at 550° C. for 4 hours to obtain the desired catalyst. The propane raw material and the above-mentioned catalyst were reacted under the same conditions as in Example 1, and the results are shown in Table 1.

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Abstract

The invention relates to a catalyst for propane dehydrogenation to produce propylene, which mainly solves the problem of low selectivity of Cr-based dehydrogenation catalysts prepared in the prior art. The dehydrogenation catalyst used in the present invention includes the following components in parts by weight of the catalyst: a) 1 to 25 parts of Cr and / or W elements or their oxides; b) 0 to 5 parts of at least one of Group IA one element or its oxide; c) 0.01 to 5 parts of at least one element or its oxide selected from Group IVB of the Periodic Table of Elements; d) 69 to 96 parts of alumina carrier, which better solves this problem, It can be used in the industrial application of propane dehydrogenation.

Description

technical field [0001] The invention relates to a catalyst for producing propene by dehydrogenating propane. Background technique [0002] The catalytic dehydrogenation process is one of the commonly used preparation methods for low-carbon olefins. Generally, low-carbon alkanes are dehydrogenated to prepare corresponding olefins, and propylene is obtained by dehydrogenating the corresponding propane. Propylene is widely used. In addition to producing polypropylene, it is also used to produce acrylonitrile, propylene oxide, acrylic acid, isopropanol, etc. However, the increase in demand for polypropylene has always been the key to the increase in demand for propylene. It is expected that propylene will maintain an annual growth rate of 5% in the future. In order to make the output of propylene meet the demand for downstream derivatives, ethylene co-production and light oil (naphtha, Light diesel oil) cracking process is the method for preparing propylene and can no longer me...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/26B01J23/30C07C5/333C07C11/06
CPCB01J23/26B01J23/30C07C5/333C07C11/06Y02P20/52
Inventor 吴省缪长喜洪学思樊志贵
Owner CHINA PETROLEUM & CHEM CORP