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Catalyst for direct production of low-carbon olefins from core-shell type synthesis gas, production method and application

A low-carbon olefin and catalyst technology, which is applied in the application field of low-carbon olefin synthesis, can solve problems such as catalyst differences, and achieve the effects of short crystallization time, adjustable shell thickness, and shortened process cycle

Active Publication Date: 2017-07-28
SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Because different molecular sieve supports have different surface acidity and alkalinity and pore structure, the prepared catalysts have great differences in the direct production of light olefins from syngas

Method used

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  • Catalyst for direct production of low-carbon olefins from core-shell type synthesis gas, production method and application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] 300ml 10wt%Co(NO 3 ) 3 ·6H 2 O and 200ml 10wt% Mn(NO 3 ) 2 The solution was mixed, and then added ruthenium chloride to make the content 0.05wt%, and then it was mixed with 500ml NH 3 ·H 2 O (25-28wt%) solution is co-precipitated in parallel, and the precipitate is aged, washed and filtered to obtain a mixture of Co and Mn.

[0024] With tetrapropyl ammonium hydroxide TPAOH as structure directing agent, the molar ratio of sol is 1.0TEOS:0.25TPAOH:0.025((CH 3 ) 2 CHO) 3 Al:50H 2 O:2EtOH. These substances were sequentially added to a stainless steel reaction kettle lined with polytetrafluoroethylene, stirred at 60°C and 10 rpm for 2 hours until a bright yellow uniform sol was formed, and 150ml sol was obtained. Then add Co and Mn mixture precipitates into the sol, stir evenly, and crystallize at 120°C and 10rpm for 10h. After natural cooling, wash the filtrate repeatedly with deionized water until the pH value is 7.9, dry at 60°C for 12 hours, and roast at 450°...

Embodiment 2

[0027] 500ml 10wt%Co(NO 3 ) 3 ·6H2 O and 300ml 50wt% Mn(NO 3 ) 2 The solution is mixed, and then a certain amount of lanthanum nitrate is added to make the content 2wt%, and then it is mixed with the mixed solution with an equal volume of NH 3 ·H 2 O (25-28wt%) solution is co-precipitated in parallel, and the precipitate is aged, washed and filtered to obtain a mixture of Co and Mn.

[0028] With tetrapropyl ammonium hydroxide TPAOH as the structure-directing agent, the molar ratio of the sol is 3TEOS:0.5TPAOH:0.06((CH 3 ) 2 CHO) 3 Al:80H 2 O:5EtOH. These substances were sequentially added to a stainless steel reaction kettle lined with polytetrafluoroethylene, stirred at 80°C and 20 rpm for 4 hours until a bright yellow uniform sol was formed, and 200ml of sol was obtained. Add the precipitated Co and Mn mixture into the sol, stir evenly, and crystallize at 180°C and 30rpm for 20h. After natural cooling, wash the filtrate repeatedly with deionized water until the pH...

Embodiment 3

[0031] 350ml 15wt%Co(NO 3 ) 3 ·6H 2 O and 300ml 50wt% Mn(NO 3 ) 2 The solution was mixed, and then a certain amount of chloroplatinic acid was added to make the content 0.5wt%, and then it was mixed with the mixed solution with an equal volume of NH 3 ·H 2 O (25-28wt%) solution is co-precipitated in parallel, and the precipitate is aged, washed and filtered to obtain a mixture of Co and Mn.

[0032] With tetrapropyl ammonium hydroxide TPAOH as structure directing agent, the molar ratio of sol is 1.5TEOS:0.3TPAOH:0.03((CH 3 ) 2 CHO) 3 Al:50H 2 O:2EtOH. These substances were sequentially added to a stainless steel reaction kettle lined with polytetrafluoroethylene, stirred at 60°C and 15 rpm for 2 hours until a bright yellow uniform sol was formed, and 150ml of sol was obtained. Add the precipitated Co and Mn mixture into the sol, stir evenly, and crystallize at 120°C and 15rpm for 12h. After natural cooling, wash the filtrate repeatedly with deionized water until the...

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Abstract

A catalyst for the direct production of low-carbon olefins from core-shell syngas is composed of active components, additives and carriers, and its weight percentage is: cobalt oxide: 2.0-20%, manganese oxide 2.5-20%, metal additives oxidation The substance content is 0.05-2.0%, and the carrier is 58-95%. The present invention has high selectivity and can greatly reduce CO 2 The advantage of being selective.

Description

technical field [0001] The invention belongs to a catalyst and its preparation method and application, in particular to a catalyst for direct production of low-carbon olefins from core-shell synthesis gas, its preparation method and its application in the synthesis of low-carbon olefins. [0002] technical background [0003] Low-carbon olefins (ethylene, propylene and butene) are important petrochemical basic raw materials, and their applications are extremely wide. The main uses are as follows: ethylene is mainly used for synthetic rubber, synthetic resins (such as polystyrene, polyvinyl chloride), Fiber, ethylene oxide, explosives, ethanol, acetaldehyde, acetic acid and other organic synthesis products, and can replace acetylene to cut and weld metal, and can also be used as a fruit ripening agent. Currently, it is mainly used for synthetic resins and plastics. Propylene is mainly used to produce polypropylene (PP), acrylonitrile (AN), propylene oxide (PO), acetone, butano...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/00B01J29/076C10G2/00C07C1/04C07C11/02
Inventor 李德宝王俊刚侯博贾丽涛刘岩
Owner SHANXI INST OF COAL CHEM CHINESE ACAD OF SCI