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Fischer-Tropsch synthesis catalyst comprising composite molecular sieve, and preparation method and application thereof

A composite molecular sieve and Fischer-Tropsch synthesis technology, applied in the direction of molecular sieve catalysts, preparation of liquid hydrocarbon mixtures, physical/chemical process catalysts, etc.

Active Publication Date: 2015-02-25
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the core of its efficient conversion is still the catalytic issue related to the study of FT synthesis catalysts

Method used

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  • Fischer-Tropsch synthesis catalyst comprising composite molecular sieve, and preparation method and application thereof
  • Fischer-Tropsch synthesis catalyst comprising composite molecular sieve, and preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0063] Embodiment 1: Co-Pt / (Al 2 o 3 +HY+SAPO-11) (Based on catalyst, 15.0% Co, 0.10% Pt) catalyst preparation

[0064] Take by weighing pseudo-boehmite (with comparative example 1) 400g, HY powder 50g (in 600 ℃ of roasting 4 hours, the dry base is 0.81, Changling Catalyst Factory product) and SAPO-11 powder 50g (in 600 ℃ of roasting 4 hours Dry basis after 1 hour is 0.80, Changling Catalyst Factory product), then add the mixed solution of 457g water and 4.7ml concentrated nitric acid, after mixing, extrude on extruder. The molded carrier was dried at 120° C. for 4 hours, and the heating rate was 2° C. / min. The dried carrier was calcined at 600° C. for 4 hours, and the heating rate was 2° C. / min. The drying and roasting atmosphere is an air pressure of 0.1 MPa, and the hourly space velocity of the drying and roasting gas is 500 Nl / g-cat / h.

[0065] Weigh 20g carrier (water absorption rate 0.72), weigh 17.50g cobalt nitrate, 2.24g platinum chloride ammonia solution (concent...

Embodiment 2

[0067] Embodiment 2: Co-Pt / (Al 2 o 3 +HY+SAPO-11) (Based on catalyst, 15.0% Co, 0.10% Pt) catalyst preparation

[0068] The carrier is the same as in Example 1. Weigh 40g of carrier (water absorption rate 0.72), weigh 2.1g of ethylene glycol, dissolve in water into 28.8ml of impregnating solution a; impregnate the carrier with impregnating solution a, then bake in an oven at 120°C for 3 hours, and then cool to room temperature ;Take half of it for water absorption test, the water absorption is about 0.67. Weigh 17.50g of cobalt nitrate and 2.24g of platinum chloride ammonia solution (concentration is 1.07gPt / 100g solution). Dissolve in water to form 13.4 ml of impregnating liquid b, impregnate the rest of the carrier with impregnating liquid b, and then dry in an oven at 120°C for 4 hours and bake at 380°C for 4 hours. Catalyst C2 is obtained.

[0069] The evaluation method and operating conditions of the catalyst are the same as in Comparative Example 1. The obtained re...

Embodiment 3

[0070] Embodiment 3: Co-Pt / (Al 2 o 3 +HY+SAPO-11) (Based on catalyst, 15.0% Co, 0.10% Pt) catalyst preparation

[0071] The carrier is the same as in Example 1. Weigh 40g carrier (water absorption rate 0.72), weigh 35.0g cobalt nitrate, 4.48g platinum chloride ammonia solution (concentration is 1.07gPt / 100g solution). Dissolve in water to form 28.8 ml of impregnating solution a, impregnate the carrier with impregnating solution a, and then dry in an oven at 130° C. for 4 hours to obtain intermediate catalyst products. After cooling down to room temperature, take half of it to test the water absorption rate, and the water absorption rate is about 0.66. Weigh 1.7g of ethylene glycol and dissolve it in water to form 15.2ml of impregnating solution b; impregnate the intermediate product of the catalyst with impregnating solution b, then dry it in an oven at 140°C for 3 hours, and obtain catalyst C3 after cooling down to room temperature.

[0072] The evaluation method and oper...

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Abstract

The invention relates to a Fischer-Tropsch synthesis catalyst comprising composite molecular sieve, and a preparation method and an application thereof. The catalyst contains an active metal component selected from iron and / or cobalt, and a composite molecular sieve. The catalyst selectively contains a carrier of a heat-resistant inorganic oxide substrate. According to the catalyst as a standard, the content of the composite molecular sieve is 1-60wt%, and the content of the heat-resistant inorganic oxide substrate is 0-80%. According to the oxide, the content of the active metal component is 2-50%. The composite molecular sieve is a mixture comprising at least one non-zeolite molecular sieve and at least one zeolite molecular sieve, wherein a weight ratio of the non-zeolite molecular sieve to the zeolite molecular sieve is 0.1-90. The catalyst has high Fischer-Tropsch synthesis activity and selectivity, and has a selective cracking capacity upon heavy hydrocarbon in Fischer-Tropsch synthesis product. The catalyst can be directly used in Fischer-Tropsch synthesis reactions for producing clean liquid hydrocarbon products.

Description

field of invention [0001] The invention relates to a Fischer-Tropsch synthesis catalyst, its preparation and its application. Background technique [0002] Fischer-Tropsch synthesis (FTS, FT synthesis) refers to synthesis gas (CO+H 2 ) into hydrocarbons on a catalyst, the products include alkanes and alkenes, and by-product CO 2 , H 2 O and organic oxygen-containing compounds such as alcohols, aldehydes, acids, ketones and esters. The products can be processed to obtain high-quality liquid fuels, such as gasoline, diesel and aviation kerosene. It has been more than 80 years since the discovery of FT synthesis. South Africa began to use FT synthesis technology industrially in the 1950s and has been developing until now. [0003] Petroleum resources are depleting day by day, prices fluctuate at high levels, and people are increasingly active in finding alternative resources; while the proven reserves of coal and natural gas continue to increase, the research in the field of...

Claims

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Application Information

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IPC IPC(8): B01J29/85B01J29/80C10G2/00C07C1/04C07C9/04
Inventor 夏国富侯朝鹏孙霞吴玉晋超严振楠李明丰聂红李大东吴昊徐润
Owner CHINA PETROLEUM & CHEM CORP
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