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A kind of cobalt-based Fischer-Tropsch fixed bed catalyst for biomass synthesis gas and preparation method thereof

A fixed-bed catalyst and synthesis gas technology, applied in the preparation of liquid hydrocarbon mixtures, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of selectivity reduction and improve activity and selectivity, improve hydrothermal stability, and ensure the effect of reducing activity

Inactive Publication Date: 2016-04-13
ENERGY RES INST CO LTD HENAN ACADEMY OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The above-mentioned catalysts are mainly researched on the synthesis gas prepared from coal and natural gas as raw materials for Fischer-Tropsch synthesis, especially for biomass synthesis gas, the catalytic activity of CO hydrogenation, C 5+ Selectivity and thermal stability need to be further improved, CH 4 and CO 2 Selectivity needs to be further reduced

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0015] Embodiment 1 is prepared with the catalyst A of the inventive method

[0016] ① Take a BET method with a specific surface area of ​​210m 2 / g, 300g of γ-alumina with an average pore diameter of 15.2nm, add 5ml of concentrated nitric acid (65%, mass, the same as in the following examples) for peptization, then add 3.0g of scallop powder and 3.0g of CMC, mix and knead evenly to form a group, put Extrude hollow tooth-shaped special-shaped strips in the extruder, with a maximum outer diameter of 3.5mm, and then dry them in air at 110°C for 10 hours, and then bake them at 600°C for 8 hours to obtain a γ-alumina carrier.

[0017] ② Take 90g of the gamma-alumina carrier obtained in step ① and impregnate it in 75ml of zirconium nitrate solution with a concentration of 1.08mol / L. The impregnation time is 16h at room temperature. After drying in the air at 110°C for 10h, bake it at 750°C for 6h. A catalyst support is obtained.

[0018] 3. Take 10 g of the catalyst carrier obtai...

Embodiment 2

[0019] Embodiment 2 is prepared with the catalyst B of the inventive method

[0020] ① Take a BET method with a specific surface area of ​​182m 2 / g, 300g of γ-alumina with an average pore diameter of 14.4nm, add 6ml of concentrated nitric acid for peptization, then add 3.0g of kale powder and 4.0g of CMC, mix and knead evenly to form a group, put it into the extrusion machine to extrude hollow cylindrical strips, The maximum diameter of the periphery is 1.8 mm, and after drying in air at 110° C. for 12 hours, it is calcined at 650° C. for 6 hours to obtain a γ-alumina carrier.

[0021] ② Take 90g of the gamma-alumina carrier obtained in step ① and immerse it in 70ml of zirconium nitrate solution with a concentration of 1.16mol / L. The immersion time is 12h at room temperature. After drying in the air at 110°C for 10h, bake it at 700°C for 8h. A catalyst support is obtained.

[0022] 3. Take 10 g of the catalyst carrier obtained in step 2. and impregnate it with 0.056 g of ru...

Embodiment 3

[0023] Embodiment 3 is prepared with the catalyst C of the inventive method

[0024] ① Same as Example 1.

[0025] ② Take 90g of the gamma-alumina carrier obtained in step ① and impregnate it in 75ml of zirconium nitrate solution with a concentration of 0.32mol / L. The impregnation time is 16h at room temperature. After drying in the air at 110°C for 10h, bake it at 750°C for 6h. A catalyst support is obtained.

[0026] 3. Take 10 g of the catalyst carrier obtained in step 2. and impregnate it with 0.056 g of ruthenium trichloride (RuCl 3 ·3H 2 O), 8.62g cobalt nitrate (Co(NO 3 ) 3 ·6H 2 O) and 1.58g copper nitrate (Cu(NO 3 ) 2 ·3H 2 O) 11ml of mixed solution, impregnated at room temperature for 20h, dried in air at 110°C for 10h, and then calcined at 400°C for 5h to prepare catalyst C. Active component Co supported by catalyst C 3 o 4 The content is 15wt% of the total amount of catalyst, CuO content is 4.5wt%, RuO 2 The content is 0.30wt%, ZrO 2 The content is 3.0...

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PUM

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Abstract

The invention belongs to the biomass energy utilization technology field, and discloses a cobalt-based Fischer-Tropsch fixed bed catalyst used for biomass synthetic gas and a preparation method therefor. The catalyst is composed of the following materials, by weight, 5-15% of Co3O4, CuO with a content of being more than 0 and less than or equal to 5%, 0.1-1% of RuO2, 3-20% of ZrO2, and the balance being gamma-aluminum oxide. The preparation method is as follows: first, gamma-aluminum oxide with a BET specific area of 180-210 m<2> / g and an average pore size of 14-16 nm is weighed according to required weight, the gamma-aluminum is peptized with 1-3wt% of concentrated nitric acid, then 0.5-2wt% of a pore forming agent CMC and 0.5-2wt% of auxiliary extruding agent sesbania powder are added, after the above mixture is mixed, pinched, ground and agglomerated, strip extrusion molding is carried out, after drying and calcinations, an alumina carrier is obtained; second, ZrO2 component is loaded through a saturation impregnation method, and a catalyst carrier is obtained after drying and calcination; third, Co3O4, CuO and RuO2 components are loaded through a saturation impregnation method, and a catalyst is obtained after drying and calcination. The catalyst has high CO hydrogenation catalytic activity and C<+5> selectivity, and low CH4 and CO2 selectivity.

Description

technical field [0001] The invention belongs to the technical field of biomass energy utilization, in particular to a cobalt-based Fischer-Tropsch fixed-bed catalyst for biomass synthesis gas and a preparation method thereof. Background technique [0002] For a long time, the utilization of biomass energy resources has been dominated by direct combustion, which is not only inefficient, but also pollutes the environment. With the development of science and technology, biomass energy resources can be converted and efficiently utilized through various technologies to generate electricity and heat, or to produce biofuels, such as ethanol, biodiesel and biogas. Biomass gasification synthesis of clean fuel technology is to store in biomass and use the C, H components and heat energy obtained from solar photosynthesis to obtain high-quality, ultra-clean fuels through biomass gasification-Fischer-Tropsch synthesis. of liquid fuel. In this process, Fischer-Tropsch synthesis catalys...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/89C10G2/00
Inventor 李顺清雷廷宙朱金陵何晓峰杨延涛徐海燕
Owner ENERGY RES INST CO LTD HENAN ACADEMY OF SCI
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