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Iron-Based Catalysts for Direct Synthesis of Light Olefins from Syngas

A technology of iron-based catalysts and low-carbon olefins, applied in the direction of physical/chemical process catalysts, heterogeneous catalyst chemical elements, metal/metal oxides/metal hydroxide catalysts, etc., can solve the problem of low selectivity of low-carbon olefins, Low CO conversion rate and other issues, to achieve the effect of improving selectivity, large specific surface area, and rich pore structure

Active Publication Date: 2020-01-03
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 problem of low conversion rate of CO and low selectivity of low-carbon olefins in the product in the technology of direct synthesis of low-carbon olefins from synthesis gas in the prior art. A new method of direct synthesis of low-carbon olefins from synthesis gas is provided An iron-based catalyst for olefins, which has the advantages of high CO conversion and high selectivity for low-carbon olefins in the product

Method used

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  • Iron-Based Catalysts for Direct Synthesis of Light Olefins from Syngas
  • Iron-Based Catalysts for Direct Synthesis of Light Olefins from Syngas

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0043] Weigh 30.0 grams of ferric oxide (Fe 2 o 3 ), 15.0 grams of manganese dioxide (MnO 2 ), 15.0 grams of magnesium oxide (MgO), 34.0 grams of α-alumina (α-Al 2 o 3 ), 3.0 grams of niobium pentoxide (Nb 2 o 5 ) and 3.0 grams of tantalum pentoxide (Ta 2 o 5 ) six kinds of raw materials and 4 grams of hydroxypropyl methylcellulose powder of 4% by weight according to the total amount of raw materials, milled and mixed for 4 hours in a ball mill; gram into the ground and mixed material, and knead until soft; the kneaded material is sent into the extruder, made into a strip with a diameter of 5mm, and cut into a column with a length of 20mm, and after natural drying, Send it to the drying equipment and dry it at 120°C for 8 hours for later use; put the dried precursor into a high-temperature furnace and calcinate it at 1600°C for 5.0 hours, and after cooling, crush and sieve it into 60-80 meshes to obtain the desired compound Fe-based catalysts for direct synthesis of li...

Embodiment 2

[0045] Weigh 50.0 grams of ferric oxide (Fe 2 o 3 ), 10.0 grams of manganese dioxide (MnO 2 ), 10.0 grams of magnesium oxide (MgO), 28.0 grams of α-alumina (α-Al 2 o 3 ), 1.0 g niobium pentoxide (Nb 2 o 5 ) and 1.0 g of tantalum pentoxide (Ta 2 o 5 ) six kinds of raw materials and 2 grams of hydroxypropyl methylcellulose powder with a percentage by weight of 2% by the total amount of raw materials, milled and mixed for 4 hours in a ball mill; gram into the ground and mixed material, and knead until soft; the kneaded material is sent into the extruder, made into a strip with a diameter of 5mm, and cut into a column with a length of 20mm, and after natural drying, Send it to the drying equipment and dry it at 120°C for 8 hours for later use; put the dried precursor into a high-temperature furnace and calcinate it at 1600°C for 5.0 hours, and after cooling, crush and sieve it into 60-80 meshes to obtain the desired compound Fe-based catalysts for direct synthesis of light...

Embodiment 3

[0047] Weigh 20.0 grams of ferric oxide (Fe 2 o 3 ), 25.0 grams of manganese dioxide (MnO 2 ), 25.0 grams of magnesium oxide (MgO), 20.0 grams of α-alumina (α-Al 2 o 3 ), 5.0 grams of niobium pentoxide (Nb 2 o 5 ) and 5.0 grams of tantalum pentoxide (Ta 2 o 5 ) six kinds of raw materials and 6 grams of hydroxypropyl methylcellulose powder of 6% by weight in the total amount of raw materials, milled and mixed for 4 hours in a ball mill; gram into the ground and mixed material, and knead until soft; the kneaded material is sent into the extruder, made into a strip with a diameter of 5mm, and cut into a column with a length of 20mm, and after natural drying, Send it to the drying equipment and dry it at 120°C for 8 hours for later use; put the dried precursor into a high-temperature furnace and calcinate it at 1600°C for 5.0 hours, and after cooling, crush and sieve it into 60-80 meshes to obtain the desired compound Fe-based catalysts for direct synthesis of light olefin...

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Abstract

The invention relates to an iron-based catalyst for direct synthesis of low-carbon olefin from synthesis gas and mainly solves the problems of low CO conversion rate and low-carbon olefin selectivityin reactions for direct synthesis of low-carbon olefin from synthesis gas in the prior art. The iron-based catalyst for direct synthesis of low-carbon olefin from synthesis gas is prepared from components in parts by weight as follows: a) 18-50 parts of an iron element or oxide thereof; b) 10-25 parts of at least one element of manganese and zinc or oxide thereof; c) 10-25 parts of at least one element of magnesium and strontium or oxide thereof; d) 20-60 parts of an aluminum element or oxide thereof; e) 1-5 parts of a niobium element or oxide thereof; and f) 1-5 parts of a tantalum element oroxide thereof. With the adoption of the technical scheme, the problems are better solved and the catalyst can be applied to industrial production of direct synthesis of low-carbon olefin from the synthesis gas.

Description

technical field [0001] The invention relates to an iron-based catalyst for directly synthesizing low-carbon olefins from synthesis gas. Background technique [0002] Low-carbon olefins refer to olefins with carbon atoms less than or equal to 4. Low-carbon olefins represented by ethylene and propylene are very important basic organic chemical raw materials. With the rapid growth of my country's economy, the supply of low-carbon olefins has been in short supply for a long time. At present, the production of low-carbon olefins mainly adopts the petrochemical route of cracking light hydrocarbons (ethane, naphtha, light diesel oil). Due to the increasing shortage of global oil resources and the long-term high price of crude oil, the development of low-carbon olefins industry only relies on oil The tubular cracking furnace process with light hydrocarbons as raw materials will encounter more and more raw material problems, and the production process and raw materials of low-carbon...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/889C07C1/04C07C11/04C07C11/06C07C11/08
CPCB01J23/002B01J23/8892B01J2523/00C07C1/044B01J2523/22B01J2523/31B01J2523/56B01J2523/57B01J2523/72B01J2523/842B01J2523/24B01J2523/27C07C11/04C07C11/06C07C11/08Y02P20/52
Inventor 李剑锋陶跃武宋卫林庞颖聪
Owner CHINA PETROLEUM & CHEM CORP
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