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Fused iron catalyst for producing light olefins from syngas and preparation method and application thereof

A molten iron catalyst and low-carbon olefin technology, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, and hydrocarbon production from carbon oxides, can solve low mechanical strength and high production costs , expensive and other issues

Active Publication Date: 2010-06-30
ZHEJIANG UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

But with precious metal C S As a co-catalyst, expensive
[0005] Chinese patent ZL 03109585.2, Fe / activated carbon catalyst with activated carbon as carrier, manganese, copper, zinc, silicon, potassium, etc. %, the content of hydrocarbons in the gas phase product can reach 69.5%, and the selectivity of ethylene, propylene and butene in hydrocarbons can reach more than 68%, but the preparation process of the catalyst is complicated, the production cost is high, and the mechanical strength Low

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0085] According to magnetite powder 91.6, iron powder 2.1, alumina (Al 2 o 3 ) 1.8, potassium nitrate (KNO 3 ) 1.08, calcium carbonate (CaCO 3 )5.4, lanthanum oxide (La 2 o 3 ) 1.0 weight ratio, put into the electric melting furnace and energize for melting. The melting temperature is determined by the melting point of the material. The melting time is 4 to 5 hours. Below ℃, after cooling, the frit is crushed, ball milled and sieved to obtain a catalyst product, and the particle size of the catalyst product is 1-6 mm.

[0086] The final composition of the prepared catalyst is controlled as: the ratio of the amount of ferrous iron to ferric iron Fe 2+ / Fe 3+ is 0.54, the iron oxide content is 93.7%, alumina (Al 2 o 3 )1.8%, potassium oxide (K 2 O) 0.5%, calcium oxide (CaO) 3.0%, lanthanum oxide (La 2 o 3 ) 1.0%. The XRD measurement results show that the phase before reduction is magnetite (Fe 3 o 4 ). At a syngas space velocity of 12600h -1 , pressure P=1.4MPa,...

Embodiment 2

[0088] According to magnetite powder 73.1, iron powder 21.8, alumina (Al 2 o 3 ) 1.0, potassium nitrate (KNO 3 ) 2.15, calcium carbonate (CaCO 3 ) 2.7, samarium oxide (Sm 2 o 3) 1.5 weight ratio, put into the electric melting furnace and energize for melting. The melting temperature is determined by the melting point of the material. The melting time is 4 to 5 hours. Below ℃, after cooling, the frit is crushed, ball milled and sieved to obtain a catalyst product, and the particle size of the catalyst product is 10-300 microns.

[0089] The final composition of the prepared catalyst is controlled as: the ratio of the amount of ferrous iron to ferric iron Fe 2+ / Fe 3+ 8.40, the iron oxide content is 95.0%, alumina (Al 2 o 3 ) 1.0%, potassium oxide (K 2 O) 1.0%, calcium oxide (CaO) 1.5%, samarium oxide (Sm 2 o 3 ) 1.5%. The XRD results show that the phase before reduction is wustite (Fe 1-x O). At a syngas space velocity of 8400h -1 , pressure P=2.0MPa, reaction te...

Embodiment 3

[0091] According to magnetite powder 102.2, graphite powder 2.8, alumina (Al 2 o 3 ) 3.5, potassium nitrate (KNO 3 ) 3.27, calcium carbonate (CaCO 3 )3.6, cerium oxide (Ce 2 o 3 ) 0.6 weight ratio after mixing, put it into an intermediate frequency furnace and energize it for melting. The melting temperature is controlled at 2000°C. Crushing, ball milling and sieving to obtain a catalyst product, the particle size of the catalyst product is 10-300 microns.

[0092] The final composition of the prepared catalyst is controlled as: Fe 2+ / Fe 3+ is 1.96, the iron oxide content is 92.4%, alumina (Al 2 o 3 )3.5%, potassium oxide (K 2 O) 1.5%, calcium oxide (CaO) 2.0%, cerium oxide (Ce 2 o 3 )0.6%. Wherein, the carbon or graphite powder added in the raw material volatilizes in the form of carbon oxide during melting, therefore, the final composition of the catalyst does not contain this substance. The XRD measurement results show that the phase before reduction is magnet...

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Abstract

The invention provides fused iron catalyst for producing light olefins from syngas and a preparation method and application thereof. The fused iron catalyst includes iron oxide and cocatalyst and the proportion of the components is as follows by weight percent: 0.1-5 alumina, 0.1-6 potassium oxide, 0.1-4.0 calcium oxide and 0.01-8.5 other oxides, and balance iron oxide. The fused iron catalyst has the beneficial effects that (1) the materials of the fused iron catalyst are cheap and easy to get, the preparation process is simple, and the fused iron catalyst is low in cost and is suitable for industrial production; (2) the fused iron catalyst is of high mechanical strength as well as good pressure resistance and abrasion resistance and is suitable for a fixed bed, a fluidized bed and a slurry bed reactor; and (3) the fused iron catalyst has high Fischer-Tropsch synthesis activity and selectivity, the conversion per pass can be more than 95%, the selectivity of the methane is less than 10% and the content of the light olefins can reach 80-90%.

Description

(1) Technical field [0001] The invention relates to a molten iron catalyst for producing low-carbon olefins from syngas and its preparation and application. (2) Background technology [0002] Fischer-Tropsch synthesis is a polymerization process in which carbonaceous raw materials (such as coal, natural gas, biomass, etc.) are gasified into synthesis gas, which is then converted into gasoline, diesel, naphtha and other hydrocarbon products through catalysts. [0003] Low-carbon olefins, such as ethylene, propylene and butene, are used as raw materials for the production of many chemicals, and play a pivotal role in the modern petroleum and chemical industries. With the development of the economy and the progress of society, the demand is increasing day by day, and the application fields growing. Olefins are usually produced by cracking petroleum. Due to limited petroleum resources and high prices, the cost of producing olefins from petroleum resources continues to increase...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/83C07C1/04
Inventor 刘化章杨霞珍
Owner ZHEJIANG UNIV OF TECH
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