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Catalyst carrier and catalyst as well as preparation method thereof

A catalyst carrier and catalyst technology, applied in the direction of catalyst activation/preparation, catalyst carrier, chemical instruments and methods, etc., can solve the problem of easy deactivation of catalysts, achieve the effects of reducing selectivity, increasing surface area, and reducing carbon deposition

Inactive Publication Date: 2009-11-25
EAST CHINA UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0013] The technical problem to be solved by the present invention is to overcome the defect that the existing catalyst for hydrogen production by catalytic reforming of bio-oil is easily deactivated due to the easy sintering and carbon deposition of the active components, and provides a catalyst carrier and a catalyst, and their preparation methods

Method used

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  • Catalyst carrier and catalyst as well as preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] Embodiment 1 Catalyst NiO / CaO-Al 2 o 3 preparation of

[0035] Alumina pretreatment: Grind activated alumina pellets into powder in a pulverizer, put them in a muffle furnace for calcination at 800°C for 18 hours.

[0036] Catalyst support CaO-Al 2 o 3 Preparation: 52.57g Ca(NO 3 ) 2 4H 2 O plus distilled water to make Ca 2+ Aqueous solution with a concentration of 0.8mol / L, heated to 50°C, and then adding 50g of pretreated Al 2 o 3 The powder is stirred and impregnated at constant temperature for 6 hours, and then the impregnated mixture is dried in an oven at 105°C for 12 hours until the water is evaporated, cooled, then placed in a muffle furnace for calcination at 900°C for 14 hours, and crushed. The loading amount of CaO after calcination is 20% of the weight of the catalyst carrier.

[0037] Catalyst NiO / CaO-Al 2 o 3 Preparation: 10.23g Ni(NO 3 ) 2 ·6H 2 O plus distilled water to make Ni 2+ The aqueous solution with a concentration of 0.8mol / L is hea...

Embodiment 2

[0038] Embodiment 2 Catalyst NiO / CeO 2 -Al 2 o 3 preparation of

[0039] Alumina pretreatment: Grind activated alumina pellets into powder in a pulverizer, put them in a muffle furnace for calcination at 900°C for 12h.

[0040] Catalyst support CeO 2 -Al 2 o 3 Preparation: 31.52g Ce(NO 3 ) 3 ·6H 2 O plus distilled water to make Ce 3+ Aqueous solution with a concentration of 0.8mol / L, heated to 40°C, and then adding 50g of pretreated Al 2 o 3 Powder, stirred and impregnated at constant temperature for 7 hours, then dried the impregnated mixture in an oven at 105°C for 15 hours until the moisture was evaporated, cooled, then placed in a muffle furnace for calcination at 800°C for 12 hours, and then pulverized. Calcined CeO 2 The loading amount is 20% of the mass of the catalyst carrier.

[0041] Catalyst NiO / CeO 2 -Al 2 o 3 Preparation: 21.60g Ni(NO 3 ) 2 ·6H 2 O plus distilled water to make Ni 2+ Concentration of 0.8mol / L aqueous solution, heated to 60 ° C, ...

Embodiment 3

[0042] Embodiment 3 Catalyst NiO / CaO-La 2 o 3 -Al 2 o 3 preparation of

[0043] Alumina pretreatment: Grind activated alumina pellets into powder in a pulverizer, put them in a muffle furnace for calcination at 850°C for 15h.

[0044] Catalyst support CaO-La 2 o 3 -Al 2 o 3 Preparation: 28.04g Ca(NO 3 ) 2 4H 2 O and 26.57g La(NO 3 ) 3 ·6H 2 O plus distilled water to make Ca 2+ +La 3+ Aqueous solution with a concentration of 0.8mol / L, heated to 60°C, and then adding 50g of pretreated Al 2 o 3 Powder, stirred and impregnated at constant temperature for 8 hours, then dried the impregnated mixture in an oven at 110°C for 21 hours until the moisture was evaporated, cooled, then placed in a muffle furnace for calcination at 850°C for 16 hours, and then pulverized. After calcination, the loading of CaO was 10% of the mass of the catalyst support, La 2 o 3 The loading amount is 15% of the mass of the catalyst carrier.

[0045] Catalyst Ni / CaO-La 2 o 3 -Al 2 o 3...

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Abstract

The invention discloses a catalyst carrier, which includes aluminum oxide and oxide loaded on the aluminum oxide, the oxide loaded on the aluminum oxide is alkaline earth oxide and / or lanthanide metallic oxide. The invention also discloses a catalyst, which includes catalyst carrier according to the invention, and substance with catalytic activity loaded on the catalyst carrier. The catalyst is used for hydrogen production from biological oil wit high catalytic activity, and can improve selectivities of product hydrogen gas and carbon dioxide, and reduce selectivity of by-product methane with reduced carbon deposit, further improve productivity of hydrogen gas. The invention also provides a preparation method of catalyst carrier and a preparation method of catalyst.

Description

technical field [0001] The invention relates to a catalyst carrier, a catalyst and a preparation method thereof. Background technique [0002] Currently, due to CO 2 Emissions are causing global warming, and fossil resources are becoming increasingly depleted, and global research on the use of renewable energy continues to rise. Hydrogen is an environmentally friendly and clean energy that can be used in fuel cells for vehicles. Compared with other types of power generation systems, fuel cells have higher power generation efficiency. There are many methods for producing hydrogen from fossil fuels, such as naphtha, natural gas and coal, as raw materials. Ultimately, however, reductions in greenhouse gas emissions can only be achieved ultimately through the production of hydrogen from renewable resources such as biomass. Biomass has the characteristics of abundant resources, renewable, and environment-friendly. Existing renewable hydrogen energy is usually obtained from bio...

Claims

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Application Information

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IPC IPC(8): B01J32/00B01J23/755B01J23/42B01J23/44B01J23/46B01J37/02B01J37/08C01B3/22
Inventor 蓝平许庆利黄慨颜涌捷张素平张尤华隋淼
Owner EAST CHINA UNIV OF SCI & TECH