Method for preparing single-atom, atomic cluster or single-molecular catalyst for oxidative coupling of methane using chemical vapor deposition

Patent metadata

Field	Value
Publication number	US-12544749-B2
Application number	US-202218079568-A
Country	US
Kind code	B2
Filing date	Dec 12, 2022
Priority date	Dec 13, 2021
Publication date	Feb 10, 2026
Grant date	Feb 10, 2026

Abstract

According to various aspects and exemplary embodiments of the present disclosure, ultra-small catalyst particles having extremely high reactivity may be synthesized in single-atom or single-molecule state. When the ultra-small-sized single-atom or single-molecule catalyst is used, the use of metal raw materials can be minimized and, at the same time, catalytic activity may be maximized through maximized reactivity of the single-atom or single-molecule catalyst.

First claim

What is claimed is:

1 . A method for preparing a M-M′ catalyst for oxidative coupling of methane, comprising: (a1) a step of depositing a solution of a precursor of a M′ catalyst on a support and then drying the same to obtain a dried catalyst, (a2) a step of obtaining a M′ catalyst deposited on the support by removing the functional groups of the precursor of a M′ catalyst through heat treatment of the dried catalyst, (b) a step of locating the M′ catalyst deposited on the support in a reactor, (c) a step of locating the precursor of a M metal in an evaporator, (c′) a step of supplying a gas for creating a gas atmosphere in the reactor into the reactor, (c″) a step of supplying a gas for creating a gas atmosphere in the evaporator into the evaporator, (d) a step of heating the reactor to a reaction temperature, (e) a step of heating the evaporator to an evaporation temperature, (f) a step of supplying a carrier gas to the evaporator and depositing a single M metal atom on the M′ catalyst deposited on the support by transporting the carrier gas to the reactor via a gas tube connected to the evaporator, (f′) a step of interrupting the flow of the carrier gas transported to the reactor and supplying an inert carrier gas selected from nitrogen, argon, helium and mixtures thereof into the reactor, and (g) a step of preparing a M-M′ catalyst by alloying the support with the single M metal atom deposited and the deposited M′ catalyst through alloying heat treatment; and wherein the M′ catalyst is a manganese (Mn) catalyst, a cerium (Ce) catalyst, or a mixture thereof; wherein the M is tungsten (W); and wherein in step (d), the reactor is heated to a reaction temperature selected within a range of 180-200° C. at a rate of 1-9° C./min, and, in step (e), the evaporator is heated to an evaporation temperature selected within a range of 90-100° C. at a rate of 1-9° C./min.

2 . The method for preparing a M-M′ catalyst for oxidative coupling of methane according to claim 1 , wherein
the gas for creating a gas atmosphere in the reactor or the carrier gas is an inert carrier gas selected from nitrogen, argon, helium and mixtures thereof, or a reactive carrier gas with oxygen or hydrogen included in the inert carrier gas, and
the gas for creating a gas atmosphere in the evaporator is an inert carrier gas selected from nitrogen, argon, helium and mixtures thereof, or a reactive carrier gas with oxygen or hydrogen included in the inert carrier gas.

3 . The method for preparing a M-M′ catalyst for oxidative coupling of methane according to claim 1 , wherein, in the step (g), the alloying heat treatment is performed under a gas atmosphere selected from air, oxygen, hydrogen and mixtures thereof at 400-1,200° C. for 1-6 hours.

4 . The method for preparing a M-M′ catalyst for oxidative coupling of methane according to claim 1 , wherein
the support is a powder or plate support, and
the support comprises 0.1-20 wt % of a sodium (Na) component based on the total weight of the support and the sodium component.

5 . The method for preparing a M-M′ catalyst for oxidative coupling of methane according to claim 1 , wherein the support is a support selected from: a ceramic-based support selected from silica gel, silica powder, alumina, zirconia, titania, zeolite and mixtures thereof; a metal-based support which is a metal plate, a metal foil or a combination thereof; a carbon-based support selected from carbon black, activated carbon, graphene, carbon nanotube, graphite and mixtures thereof; a transparent electrode; and combinations thereof.

6 . The method for preparing a M-M′ catalyst for oxidative coupling of methane according to claim 1 , wherein, in the step (b), the M′ catalyst deposited on the support is located on an amorphous material or a porous filter provided at the center of the reactor.

7 . The method for preparing a M-M′ catalyst for oxidative coupling of methane according to claim 1 , wherein, in the step (f), the carrier gas is supplied at a rate of 10-90 sccm for 1-240 minutes.

8 . The method for preparing a M-M′ catalyst for oxidative coupling of methane according to claim 1 , wherein the precursor is W(CO) 6 and the evaporation temperature is 80-100° C.

9 . The method for preparing a M-M′ catalyst for oxidative coupling of methane according to claim 1 , wherein
the precursor is W(CO) 6 ,
in the step (d), the reactor is heated to a reaction temperature selected within a range of 150-250° C. at a rate of 0.1-9° C./min,
in the step (e), the evaporator is heated to an evaporation temperature selected within a range of 80-150° C. at a rate of 0.1-9° C./min,
in the step (f), the carrier gas is supplied at a rate of 20-100 sccm for 20-240 minutes, and
the alloying heat treatment is performed under air atmosphere at 700-900° C. for 3-5 hours.

Assignees

• Korea Inst Energy Res

Inventors

• Kim Hee-Yeon
• Choi Yoonseok
• Kim Tae-Woo
• Yu Ji-Haeng
• Kim Cha-Heon

Classifications

• B01J23/34

  Manganese · CPC title

• B01J37/08

  Heat treatment {(B01J37/0009, B01J37/0018 take precedence)} · CPC title

• B01J21/08

  Silica · CPC title

• B01J37/0244

  Coatings comprising several layers · CPC title

• B01J23/30

  Tungsten · CPC title