Iron-based catalyst for preparing low-carbon alkane as well as preparation method and using method of iron-based catalyst for preparing low-carbon alkane

A technology of iron-based catalysts and low-carbon olefins, applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxides/metal hydroxide catalysts, etc., can solve low-carbon olefins low selectivity, strength, Poor thermal stability, low conversion rate of CO, etc., to achieve the effect of improving selectivity, good thermal stability, and reducing internal diffusion resistance

Active Publication Date: 2015-03-25
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] The technical problem to be solved by the present invention is the problem of low CO conversion rate and low selectivity of low-carbon olefins in the product in the Fischer-Tropsch synthesis process of low-carbon olefins in the prior art, and the problem of poor strength and thermal stability of the catalyst under the conditions of use. Provide a new iron-based catalyst for preparing low-carbon olefins, which has the advantages of high conversion rate of CO and high selectivity of low-carbon olefins in the product when the catalyst is used for Fischer-Tropsch synthesis of low-carbon olefins

Method used

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  • Iron-based catalyst for preparing low-carbon alkane as well as preparation method and using method of iron-based catalyst for preparing low-carbon alkane
  • Iron-based catalyst for preparing low-carbon alkane as well as preparation method and using method of iron-based catalyst for preparing low-carbon alkane

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Weigh 55.0 grams of iron oxide (Fe 2 o 3 ), 5.0 grams of cobaltous oxide (CoO), 17.0 grams of molybdenum oxide (MoO 3 ), 10.0 grams of magnesium oxide (MgO), 10.0 grams of tin oxide (SnO 2 ) and 3.0 g of scandium oxide (Sc 2 o 3 ) Six kinds of raw materials and 3 grams of scallop powder with a weight percentage of 3% by weight of the total amount of raw materials were mixed in a ball mill for 2 hours; The kneaded material is kneaded 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. After natural drying, it is sent to the drying equipment , dried at 120°C for 8 hours for later use; put the dried precursor into a high-temperature furnace, calcined at 1200°C for 4.0 hours, and after cooling, crush and sieve into 60-80 meshes to obtain the required synthesis gas for low-carbon production Iron-based catalysts for olefins. The prepared catalyst comprises the following compon...

Embodiment 2

[0031] Weigh 78.0 grams of iron oxide (Fe 2 o 3 ), 0.7 grams of cobaltous oxide (CoO), 6.5 grams of molybdenum oxide (MoO 3 ), 3.2 grams of magnesium oxide (MgO), 3.2 grams of tin oxide (SnO 2 ) and 8.4 g of scandium oxide (Sc 2 o 3 ) Six kinds of raw materials and 3 grams of scallop powder with a weight percentage of 3% by weight of the total amount of raw materials were mixed in a ball mill for 2 hours; The kneaded material is kneaded 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. After natural drying, it is sent to the drying equipment , dried at 120°C for 8 hours for later use; send the dried precursor into a high-temperature furnace, calcined at 1000°C for 4.0 hours, and after cooling, crush and sieve into 60-80 meshes to obtain the required synthesis gas for low-carbon production Iron-based catalysts for olefins. The prepared catalyst comprises the following componen...

Embodiment 3

[0034] Weigh 30.0 grams of iron oxide (Fe 2 o 3 ), 20.0 grams of cobaltous oxide (CoO), 37.0 grams of molybdenum oxide (MoO 3 ), 4.0 grams of magnesium oxide (MgO), 4.0 grams of tin oxide (SnO 2 ) and 5.0 g of scandium oxide (Sc 2 o 3 ) Six kinds of raw materials and 3 grams of scallop powder with a weight percentage of 3% by weight of the total amount of raw materials were mixed in a ball mill for 2 hours; The kneaded material is kneaded 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. After natural drying, it is sent to the drying equipment , dried at 120°C for 8 hours for later use; put the dried precursor into a high-temperature furnace, calcined at 1400°C for 4.0 hours, and after cooling, crush and sieve into 60-80 meshes to obtain the required synthesis gas to produce low-carbon Iron-based catalysts for olefins. The prepared catalyst comprises the following components ...

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Abstract

The invention relates to an iron-based catalyst for preparing low-carbon alkane as well as a preparation method and a using method of the iron-based catalyst for preparing the low-carbon alkane. The iron-based catalyst for preparing the low-carbon alkane is mainly used for solving the problems that the reaction of preparing low-carbon alkane from a synthesis gas in the prior art is low in CO conversion rate and low in low-carbon alkane selectivity, and the catalyst is poor in strength and thermal stability under a using condition. The problems are solved very well by adopting a technical scheme that the catalyst comprises the following components in parts by weight: a) 20-80 parts of an iron element or oxides thereof; b) 1-15 parts of a cobalt element and oxides thereof; c) 10-30 parts of at least one element selected from molybdenum and vanadium or oxides thereof; d) 5-20 parts of at least one element selected from magnesium and barium or oxides thereof; e) 5-20 parts of at least one element selected from tin and aluminum or oxides thereof; and f) 0.5-10 parts of a scandium element or oxides thereof. The catalyst can be used for industrial production of preparing low-carbon alkane from the synthesis gas by virtue of a one-step process.

Description

technical field [0001] The invention relates to an iron-based catalyst for preparing low-carbon olefins, a preparation method and a use method thereof. 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 materia...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/887B01J23/847C07C1/04C07C11/02
Inventor 李剑锋陶跃武宋卫林庞颖聪
Owner CHINA PETROLEUM & CHEM CORP
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