Fe/pressed active carbon catalyst and preparation method thereof

A technology for shaping activated carbon and catalysts, applied in physical/chemical process catalysts, chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of increasing raw material costs and operating costs, increasing costs and burdens, Catalyst activity and selectivity and other performance degradation problems, to achieve the effect of improving catalytic performance and stability, preventing collapse and expansion, and inexpensive raw materials

Inactive Publication Date: 2009-07-15
BEIJING UNIV OF CHEM TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the iron salt and manganese salt of the auxiliary agent used in the preparation of the catalyst are more expensive and insoluble iron oxalate and manganese acetate, and ethanol is used as the solvent at the same time, which will inevitably increase the cost of raw materials and operating cost
Moreover, during the reshaping process necessary for the catalyst to be used in industrial production, the performance of the catalyst, such as activity and selectivity, will inevitably decrease, increasing the cost and burden of production.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0033] A. According to the mass percentage of elements: Fe=53.8wt%, Mn=38.5wt%, Li=7.7wt%, weigh 10.8214g iron nitrate, 3.4934g manganese nitrate, 2.1161g lithium nitrate, dissolve in 20ml water to make a solution , add a drop of dispersant AEO-3, stir to prepare impregnation solution;

[0034] Divide the impregnating solution into three groups according to the volume ratio of 2:2:1.

[0035] B. Under vacuum conditions, immerse 1.5004g of compressed fruit shell charcoal into the first group of solutions, mix and stir evenly, place in an oven and dry at 50°C for 72 hours, and dry the obtained material in 20ml / min of flowing nitrogen Under protection, calcined at 100°C for 0.5 hours, calcined at 300°C for 3 hours, and passivated for 24 hours.

[0036] C. impregnating the material obtained after step B is dried into the second group of solutions; other steps are the same as step B;

[0037] Then the material obtained by drying is impregnated with the third group of solutions, a...

Embodiment 2

[0040] A. According to the mass percentage of elements: Fe=41.67wt%, Mn=41.67wt%, Mg=8.33wt%, Cu=8.33wt% Weigh 6.241g iron oxalate, 4.8818g manganese nitrate, 3.1985g magnesium nitrate, 1.1291 g copper nitrate, dissolved in 30ml of water and ethanol mixture to make a solution (water:ethanol=2:1), and stirred to make an impregnating solution;

[0041] Divide the impregnating solution into four groups according to the volume ratio of 1:1:1:1.

[0042] B. Under vacuum conditions, immerse 2.4016g of extruded coconut shell charcoal in the first group of solutions, mix and stir evenly, and place in an oven to dry at 90°C for 24 hours. The material obtained after drying was calcined at 400° C. for 2 hours under the protection of flowing helium gas at 20 ml / min, and then passivated for 24 hours.

[0043] C. impregnating the material obtained after step B is dried into the second group of solutions; other steps are the same as step B;

[0044] D. Immerse the material obtained after s...

Embodiment 3

[0048] A. According to element mass percentage content: Fe=71.44wt%, Mn=14.28wt%, Na=7.14wt%, Ca=7.14wt% Weigh 10.8225g ferric nitrate, 0.9758g manganese nitrate, 0.6909g sodium carbonate, 0.8845 g calcium nitrate, dissolved in 20ml water to make a solution, stirred to make an impregnating solution;

[0049] Divide the impregnating solution into three groups according to the volume ratio of 2:2:1.

[0050] B. Under vacuum conditions, immerse 0.6092g of petal shell charcoal into the first group of solutions, mix and stir evenly, and dry naturally at 25-30°C for 150 hours. The material obtained after drying was calcined at 400° C. under the protection of 20 ml / min flowing argon for 1 hour, and then passivated for 24 hours.

[0051] C. impregnating the material obtained after step B is dried into the second group of solutions; other steps are the same as step B;

[0052] Then the material obtained by drying is impregnated with the third group of solutions, after drying, it is c...

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Abstract

The invention discloses a catalytic conversion agent of tar in gas for a biomass boiler, which consists of the following ingredients by weight percent: 0.1% to 0.3% of Na2CO3, 0.1% to 0.3% of K2CO3, 0.1% to 1% of Fe3O4, 0.5% to 0.8% of NaCl, 0.5% to 0.8% of KCl, 0.3% to 0.5% of KOH, 0.3% to 0.5% of NaOH, 0.1 to 1% of Ni(NO3)2 6H2O, 0.1 to 1% of KNO3, 0.1 to 0.5% of Ce(NO3)3 6H2O, 20% to 46% of dry attapulgite powder and 46% to 75% of dry dolomite powder, wherein the dry dolomite powder is the dry powder with the grain size not less than 325 meshes, the water content less than 1% and the CaCO3/MgCO3 ratio ranging from 1 to 1.5, and the dry attapulgite powder has the grain size not less than 325 meshes, the water content is less than 1%, the content of MgO is not less than 23% and the content of SiO2 is not more than 56%. By using the catalyst, tar in biomass gasified gas can be converted into combustible small molecules, so as to reduce the hazard caused by tar remarkably.

Description

technical field [0001] The invention provides a Fe / formed activated carbon catalyst and a preparation method thereof, the catalyst is suitable for synthesis gas CO+H 2 Direct conversion to low carbon olefins - the preparation process of ethylene, propylene and butene. Background technique [0002] At present, the fuel consumed in the world and the raw materials required for chemical production mainly depend on petroleum. In recent years, due to the shrinking of oil reserves and the continuous rise of oil prices, it is unavoidable to search for alternative energy sources of oil. The development of a process route for preparing chemical raw materials from non-petroleum resources has attracted the attention of countries all over the world, especially developed countries. Low-carbon olefins represented by ethylene and propylene are the most basic raw materials in the chemical industry and play a pivotal role in the modern petroleum and chemical industries. Syngas is a mixed ga...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/745B01J23/889C07C1/04
Inventor 张敬畅李根曹维良
Owner BEIJING UNIV OF CHEM TECH
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