A preparing method of a catalyst used for preparing low-carbon olefins from synthetic gas and applications of the catalyst

A low-carbon olefin and catalyst technology, which is applied in the field of catalyst preparation, can solve the problems of wide catalyst particle size distribution, reduced synthesis gas utilization rate, low product added value, etc., and achieves good reaction product distribution, improved utilization rate, and short cycle time. Effect

Inactive Publication Date: 2014-08-20
NINGXIA UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The above catalytic systems have made good progress in the synthesis of low-carbon olefins and obtained high selectivity of low-carbon olefins, but the catalyst preparation methods are mostly chemical methods such as impregnation and coprecipitation, and the catalyst particle size distribution is wide. Long cycle, high cost, poor repeatability; relatively wide product distribution, low product added value; CO 2 、CH 4 The selectivity is high, which reduces the utilization rate of synthesis gas

Method used

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  • A preparing method of a catalyst used for preparing low-carbon olefins from synthetic gas and applications of the catalyst
  • A preparing method of a catalyst used for preparing low-carbon olefins from synthetic gas and applications of the catalyst

Examples

Experimental program
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Effect test

Embodiment 1

[0025] Weigh Fe(NO 3 ) 3 9H 2 O40.25g, ZrO(NO 3 ) 2 2H 2 O4.44g, Zn(NO 3 ) 2 ·6H 2 03.66g is mixed with homogeneous mixed solution 100mL, is precipitating agent with urea, takes by weighing urea 21.42g, adds in the prepared homogeneous mixed solution and stirs; The mixed solution that stirs is transferred in the dissolving cup of TFM material, in Microwave 2450MHz, pressure 1.5MPa, power 300W, heat for 180min, drop to room temperature, suction filter, wash the obtained precipitate until neutral, dry at 50℃ overnight, roast in a muffle furnace at 350℃ for 6h to obtain powder A; weigh 5g Powder A, 0.15g K 2 CO 3 , Measure 5g of powder A saturated water absorption volume of distilled water will be weighed K 2 CO 3 Prepare a solution, impregnate 5 g of powder with equal volume, and dry in an oven at 60°C after impregnation to obtain powder B. Grind B, tablet and granulate it to 20-40 mesh to obtain a catalyst.

[0026] The application process of the catalyst used to pr...

Embodiment 2

[0029] Weigh Fe 2 (C 2 o 4 ) 3 ·5H 2 O16.47g, Zr(NO 3 ) 4 ·5H 2 O15.18g, Zn(NO 3 ) 2 ·6H 2 07.32g is mixed with homogeneous mixed solution 100mL, is precipitating agent with urea, takes by weighing urea 19.94g, adds in the prepared homogeneous mixed solution and stirs; The mixed solution that stirs is transferred in the dissolving cup of TFM material, in Microwave 2450MHz, pressure 2MPa, power 400W, heat for 150min, drop to room temperature, suction filter, wash the obtained precipitate until neutral, dry overnight at 80℃, then roast in a muffle furnace at 550℃ for 3h to obtain powder A; weigh 5g of powder A, 0.22g K 2 CO 3 , Measure 5g of powder A saturated water absorption volume of distilled water will be weighed K 2 CO 3 Prepare a solution, impregnate 5 g of powder with equal volume, and dry in an oven at 90°C after impregnation to obtain powder B. Grind, tablet and granulate B to 20-40 mesh to obtain a catalyst.

[0030] The application process of the cataly...

Embodiment 3

[0033] Weigh Fe 2 (C 2 o 4 ) 3 ·5H 2 O8.80g, ZrOCl 2 ·8H 2 O18.26g, Zn(NO 3 ) 2 ·6H 2 03.66g is mixed with homogeneous mixed solution 100mL, is precipitating agent with urea, takes by weighing urea 15.09g, adds in the prepared homogeneous mixed solution and stirs; The mixed solution that stirs is transferred in the dissolving cup of TFM material, in Microwave 2450MHz, pressure 2.5MPa, power 500W, heat for 60min, drop to room temperature, suction filter, wash the obtained precipitate until neutral, dry overnight at 120°C, roast in a muffle furnace at 450°C for 5h to obtain powder A; weigh 5g Powder A, 0.3g K 2 CO 3 , Measure 5g of powder A saturated water absorption volume of distilled water will be weighed K 2 CO 3 Prepare a solution, impregnate 5 g of powder with equal volume, and dry in an oven at 120°C after impregnation to obtain powder B. Grind, tablet and granulate B to 20-40 mesh to obtain a catalyst.

[0034] The application process of the catalyst used to...

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Abstract

The invention relates to a preparing method of a catalyst used for preparing low-carbon olefins from synthetic gas and applications of the catalyst. Active components of the catalyst are Fe and Zr. Assistants of the catalyst are Zn and K. The catalyst comprises 20-80 wt% of the Fe, 20-80 wt% of the Zr, 5-20 wt% of the Zn, and 0.5-5 wt% of the K. The catalyst is prepared by a microwave hydrothermal method and a dipping method. Urea is adopted as a precipitator. An active component ferric salt is one selected from ferric nitrate and ferric oxalate. A zircon salt is one selected from zirconium oxychloride, zirconium nitrate and zirconium oxynitrate. An assistant zinc salt is selected from zinc nitrate and a potassium salt is selected from potassium carbonate. Compared with the prior art, the catalyst has characteristics of cheap and easily available raw materials, simple preparation process, short cycle, low energy consumption, good repeatability, low cost and suitability for industrial production. The CO conversion per pass is higher than 93%. The olefin-alkyl (O/P) ratio is higher than 4.80. The yield of C2-C4 olefins can reach 68.15-72.38 g/[m<3>(CO+H2)]. CH4, CO2 and C<5><+> can be maintained in a relatively low value. The reaction products are well distributed. The utilization rate of the synthetic gas is increased.

Description

technical field [0001] The invention belongs to the fields of energy and chemical industry, and in particular relates to a preparation method and application of a catalyst for preparing low-carbon olefins from syngas. Background technique [0002] Low-carbon olefins generally refer to olefins with carbon atoms less than or equal to 4, such as ethylene, propylene, and butene. Low-carbon olefins are important basic organic chemical raw materials for the production of polyethylene, polypropylene, Organic compounds such as acrylonitrile, ethylene oxide or ethylene glycol occupy a very important position in the national economy, and the demand is increasing day by day. At present, low-carbon olefins mainly come from the petrochemical route of cracking naphtha or light diesel oil. With the depletion of petroleum resources, oil prices are rising day by day, resulting in the continuous increase of production costs of low-carbon olefins, while coal, natural gas and biomass resources ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/80C07C11/02C07C11/04C07C11/06C07C11/08C07C1/04
CPCY02P20/52
Inventor 张建利赵天生高新华范素兵陈宁
Owner NINGXIA UNIVERSITY
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