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Iron catalyst for preparing light olefins by use of synthesis gas and preparation method of iron catalyst

A technology of carbon olefin iron and low-carbon olefins, which is applied in the field of synthesis gas to low-carbon olefin iron catalysts and its preparation, can solve the problems of low selectivity of low-carbon olefins and low CO conversion rate, and achieve improved selectivity and thermal stability Good sex and stable effect

Active Publication Date: 2015-04-29
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 provides a new iron catalyst for the production of low-carbon olefins from synthesis gas , when the catalyst is used in Fischer-Tropsch synthesis of low-carbon olefins, it has the advantages of high conversion rate of CO and high selectivity of low-carbon olefins in the product

Method used

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  • Iron catalyst for preparing light olefins by use of synthesis gas and preparation method of iron catalyst
  • Iron catalyst for preparing light olefins by use of synthesis gas and preparation method of iron catalyst

Examples

Experimental program
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Effect test

Embodiment 1

[0028] Weigh 55.0 grams of iron oxide (Fe 2 o 3 ), 16.0 grams of titanium oxide (TiO 2 ), 16.0 grams of molybdenum oxide (MoO 3 ), 5.0 grams of vanadium pentoxide (V 2 o 5 ), 5.0 grams of lanthanum oxide (La 2 o 3 ) and 3.0 g tin oxide (SnO 2 ) Six kinds of raw materials and 3 grams of carbon black 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; the dried precursor was sent into a high-temperature furnace, calcined at 1400°C for 6.0 hours, and after cooling, it was crushed and sieved into 60-80 meshes to obtain the required high-temperature sintered iron catalyst. The prepared catalyst comprises the following components...

Embodiment 2

[0031] Weigh 88.0 grams of iron oxide (Fe 2 o 3 ), 5.79 grams of titanium oxide (TiO 2 ), 5.79 grams of molybdenum oxide (MoO 3 ), 0.06 g vanadium pentoxide (V 2 o 5 ), 0.06 g lanthanum oxide (La 2 o 3 ) and 0.3 g tin oxide (SnO 2 ) Six kinds of raw materials and 3 grams of carbon black 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; the dried precursor was sent into a high-temperature furnace, calcined at 1400°C for 6.0 hours, and after cooling, it was crushed and sieved into 60-80 meshes to obtain the required high-temperature sintered iron catalyst. The prepared catalyst comprises the following components in weight p...

Embodiment 3

[0034] Weigh 29.2 grams of iron oxide (Fe 2 o 3 ), 12.5 grams of titanium oxide (TiO 2 ), 12.5 grams of molybdenum oxide (MoO 3 ), 18.0 grams of vanadium pentoxide (V 2 o 5 ), 18.0 grams of lanthanum oxide (La 2 o 3 ) and 9.8 g tin oxide (SnO 2 ) Six kinds of raw materials and 3 grams of carbon black 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; the dried precursor was sent into a high-temperature furnace, calcined at 1400°C for 6.0 hours, and after cooling, it was crushed and sieved into 60-80 meshes to obtain the desired high-temperature sintered catalyst. The prepared catalyst comprises the following components in ...

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Abstract

The invention relates to an iron catalyst for preparing light olefins by use of synthesis gas and a preparation method of the iron catalyst, aiming at solving the problems that CO conversion rate is low, the light olefin selectivity is low, and the catalyst has low strength and poor stability under a using condition when the synthesis gas is used for preparing the light olefins in the prior art. The iron catalyst is prepared from the following components in parts by weight: (a) 35-90 parts of iron element or oxide thereof; (b) 5-30 parts of at least one element of titanium and zirconium or oxide of at least one of titanium and zirconium; (c) 5-30 parts of at least one element of molybdenum and tungsten or oxide of at least one of molybdenum and tungsten; (d) 0.1-10 parts of at least one element of vanadium and niobium or oxide of at least one of vanadium and niobium; (e) 0.1-10 parts of at least one element of lanthanum and samarium or oxide of at least one of lanthanum and samarium; and (f) 0.5-5 parts of tin or oxide thereof. The iron catalyst can solve the above problems well and can be used for industrial production for preparing light olefins through Fischer-Tropsch synthesis.

Description

technical field [0001] The invention relates to an iron catalyst for producing low-carbon olefins from synthesis gas and a preparation 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 material...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/887B01J23/85C07C11/02C07C1/04
Inventor 李剑锋陶跃武宋卫林庞颖聪
Owner CHINA PETROLEUM & CHEM CORP
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