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Methane oxidative coupling catalyst, preparation method thereof and method for preparing ethylene through methane oxidative coupling

A technology of oxidative coupling and catalysts, which is applied in the direction of carbon compound catalysts, metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, etc., and can solve the problem that there are many reaction steps and multi-step methods are not economically reasonable choices, etc. problems, to achieve the effect of improving catalyst activity, high industrial application prospects, and simple steps

Pending Publication Date: 2021-06-01
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0004] Starting from natural gas, the three-step method of partial oxidation to synthesis gas / syngas to methanol / methanol to olefins (POM / GTM / MTO) is used to produce ethylene. Not only are there many reaction steps, but also oxygen atoms must be inserted first and then taken out, which is non-atomic. Economic response; from the aspects of technology, resource utilization, environmental protection, etc., the multi-step method is not an economically reasonable choice

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  • Methane oxidative coupling catalyst, preparation method thereof and method for preparing ethylene through methane oxidative coupling

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preparation example Construction

[0022] In the catalyst preparation method of the present invention, the calcination temperature may be, for example, 500-850° C., and the calcination time may be, for example, 2-10 hours. Preferably, the roasting process includes: heating the dried product to 600-850°C (more preferably 650-850°C) at a constant rate of 3-15°C / min (more preferably 5-10°C / min) , and incubated for 2-10 hours (more preferably incubated for 4-8 hours).

[0023] In the catalyst preparation method of the present invention, the soluble salts of manganese and gallium can be various water-soluble active component precursors, as long as various oxides of manganese and gallium oxide can be formed respectively by roasting . The soluble salt of manganese is preferably manganese nitrate, and the soluble salt of gallium is preferably gallium nitrate. The gallium nitrate usually exists in the form of its hydrate.

[0024] In the preparation method of the present invention, each active component is supported ...

Embodiment 1

[0050] Dissolve 7.03g of manganese nitrate solution in 35mL of water, add 18g of cristobalite carrier, stir at room temperature for 1h, rotate evaporate at 80°C for 2h, and dry at 110°C for 3h to obtain manganese-impregnated cristobalite.

[0051] Dissolve 0.20 g of sodium tungstate dihydrate in 20 mL of water, add cristobalite impregnated with manganese, stir at room temperature for 1 h, rotate evaporate at 80 °C for 3 h, and dry at 120 °C for 2 h to obtain cristobalite impregnated with manganese and sodium tungstate.

[0052] Dissolve 0.05g of gallium nitrate hydrate in 20mL of water, add cristobalite impregnated with manganese and sodium tungstate, stir at 50°C for 1.5h, rotate at 80°C for 2h, dry at 110°C for 3h, and then dry in air Heat up to 800°C at a rate of 5°C / min and bake for 5h. After cooling to room temperature, catalyst A1 (Na 2 WO 4 -Mn-Ga 2 o 3 / cristobalite); Wherein, based on the weight of cristobalite, the mass percentage of active component is: Na 2 WO...

Embodiment 2

[0061] Dissolve 4.68g of manganese nitrate solution in 30mL of water, add 18g of cristobalite carrier, stir at room temperature for 1h, rotary evaporate at 80°C for 2h, and dry at 150°C for 5h to obtain manganese-impregnated cristobalite.

[0062] Dissolve 1.21g of sodium tungstate dihydrate in 25mL of water, add cristobalite impregnated with manganese, stir at room temperature for 1 hour, rotate evaporate at 80°C for 2 hours, and dry at 180°C for 2 hours to obtain cristobalite impregnated with manganese and sodium tungstate.

[0063] Dissolve 0.005g of gallium nitrate hydrate in 20mL of water, add cristobalite impregnated with manganese and sodium tungstate, stir at 40°C for 1h, rotate at 80°C for 2h, dry at 150°C for 2h, and then dry in air for 5 The rate of ℃ / min was raised to 850℃ for 8h. After cooling to room temperature, catalyst A2 (Na 2 WO 4 -Mn-Ga 2 o 3 / cristobalite); Wherein, based on the weight of cristobalite, the mass percentage of active component is: Na 2 ...

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Abstract

The invention relates to the field of natural gas utilization, and discloses a methane oxidative coupling catalyst, a preparation method thereof and a method for preparing ethylene through methane oxidative coupling. The methane oxidative coupling catalyst comprises cristobalite and an active component loaded on the cristobalite, wherein the active component comprises sodium tungstate, manganese oxide and gallium oxide; in the catalyst, based on the weight of cristobalite, the content of sodium tungstate is 0.9-15 wt%, the content of manganese oxide is 0.4-6.5 wt% in terms of manganese, and the content of gallium oxide is 0.01-8 wt%. The catalyst can effectively promote the oxidative coupling reaction of methane at high temperature to generate C2 and above hydrocarbons such as ethylene. The method for preparing the catalyst is simple in step, and the catalyst has a higher industrial application prospect.

Description

technical field [0001] The invention relates to the field of utilization of natural gas, in particular to a methane oxidative coupling catalyst, a preparation method thereof and a methane oxidative coupling method for preparing ethylene. Background technique [0002] Ethylene is the most important basic organic chemical raw material. The production of ethylene has been relying on the petroleum cracking route for a long time, and the resulting environmental pollution and other problems are becoming more and more serious. In recent years, crude oil prices have continued to rise, which has triggered an increase in the price of ethylene cracking raw materials. At the same time, the supply of ethylene cracking raw materials is also very prominent. Facing this situation, countries around the world are adjusting their energy utilization structures and constantly looking for new ethylene production routes. . [0003] Natural gas is an important energy source, and its abundant reser...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/34C07C2/84C07C11/04
CPCB01J23/34C07C2/84C07C2523/34Y02P20/52
Inventor 武洁花张明森薛伟刘东兵
Owner CHINA PETROLEUM & CHEM CORP