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

A supported catalyst, catalyst technology, applied in catalysts, carbon compound catalysts, chemical instruments and methods, etc., can solve the problems of uneconomical and reasonable selection, many steps, etc., to promote the oxidative coupling reaction of methane, wide application prospects, The effect of improving content and yield

Pending Publication Date: 2021-03-26
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Starting from natural gas, if the partial oxidation to synthesis gas / synthesis gas to methanol / methanol to olefins three-step method (POM / GTM / MTO) is used to produce ethylene, not only the reaction process has many steps, but also the oxygen atom must be inserted first and then taken out. It is a non-atomic economic reaction, no matter in terms of technology, resource utilization, or environmental protection, the multi-step method is not an economically reasonable choice

Method used

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

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preparation example Construction

[0018] According to a second aspect of the present invention, the present invention provides a method for preparing a supported catalyst, the method comprising: in the presence of water, cristobalite is contacted with a soluble salt of manganese, sodium tungstate and ytterbium soluble salt, Dry and roast.

[0019] The present invention has no particular limitation on the cristobalite, which may be commercially available cristobalite, or may be prepared by calcination of amorphous silicon dioxide at high temperature. Direct selection of cristobalite as the carrier can make the prepared shaped catalyst have higher compressive strength, which is conducive to industrial scale-up and use.

[0020] According to the preparation method of the present invention, the consumption of the cristobalite, the soluble salt of manganese, sodium tungstate, and the soluble salt of ytterbium makes in the prepared catalyst, based on the weight of silicon dioxide, the content of the oxide of mangane...

Embodiment approach

[0031] According to a preferred embodiment, the preparation method comprises the following steps:

[0032] or

[0033]The cristobalite is respectively contacted with an aqueous solution of a soluble salt containing manganese and an aqueous solution containing sodium tungstate, and dried to obtain cristobalite impregnated with manganese and sodium tungstate;

[0034] (2) The cristobalite impregnated with manganese and sodium tungstate is brought into contact with a soluble brine solution containing ytterbium, followed by drying and firing.

[0035] In step (1), the carrier can be impregnated with the aqueous solution of the soluble salt containing manganese and sodium tungstate at the same time; the carrier can also be impregnated with the aqueous solution of the soluble salt containing manganese and the aqueous solution containing sodium tungstate . In the aqueous solution, the concentration of the soluble manganese salt can be, for example, 1-15% by weight, and the concentr...

Embodiment 1

[0055] Dissolve 10.73g of manganese nitrate solution in 50mL of water, add 33g of cristobalite, stir at room temperature for 1h, rotary evaporate at 80°C for 2h, and then dry at 120°C for 2h to obtain manganese-impregnated cristobalite.

[0056] Dissolve 0.037g of sodium tungstate dihydrate in 40mL of water, add cristobalite impregnated with manganese, stir at room temperature for 1 hour, rotary evaporate at 80°C for 2 hours, and then dry at 120°C for 2 hours to obtain cristobalite impregnated with manganese and sodium tungstate.

[0057] Dissolve 0.0075g of ytterbium nitrate pentahydrate in 20mL of water, add cristobalite impregnated with manganese and sodium tungstate, stir at 50°C for 1h, rotary evaporate at 80°C for 2h, then dry at 120°C for 2h, then dry in air at 5°C / min at a rate of 800°C for 5 h. After being cooled to room temperature, the obtained catalyst product is tabletted, pulverized, and sieved, and the part between 40-60 mesh is taken as catalyst A1 (Na 2 WO ...

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Abstract

The invention relates to the field of comprehensive utilization of natural gas, and discloses a supported catalyst, a preparation method thereof and a method for preparing ethylene through oxidative coupling of methane. The catalyst comprises a carrier and active components. The carrier is cristobalite, and the active components are manganese oxide, sodium tungstate and ytterbium oxide. In the supported catalyst, based on the weight of the carrier in terms of oxide, the content of manganese oxide is 0.1-6 wt% in terms of manganese, the content of sodium tungstate is 0.1-6 wt%, and the contentof ytterbium oxide is 0.005-15 wt%. The supported catalyst is used for methane conversion, can promote methane oxidative coupling reaction, keeps high stability at high temperature, and improves the methane conversion rate and the selectivity of C2 and above hydrocarbons.

Description

technical field [0001] The invention relates to the field of comprehensive utilization of natural gas, in particular to a supported catalyst, a preparation method thereof, and a method for producing ethylene through oxidative coupling of methane. Background technique [0002] Ethylene is the most important basic organic chemical raw material. For a long time, its production has been dependent on the petroleum cracking route, and the resulting environmental pollution and other problems are becoming more and more serious. In recent years, the price of crude oil has continued to rise, causing the price of ethylene cracking raw materials to rise. At the same time, the shortage of ethylene cracking raw materials is also very prominent. Faced with this situation, all countries in the world are adjusting the energy utilization structure and constantly looking for new ethylene production routes. Natural gas is an important energy source, and its abundant reserves provide a good gua...

Claims

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Application Information

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