The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
May. 14, 2024

Filed:

Oct. 28, 2022
Applicant:

SK Innovation Co., Ltd., Seoul, KR;

Inventors:

Dong Min Yun, Daejeon, KR;

Hee Soo Kim, Daejeon, KR;

Ji Hoon Lee, Daejeon, KR;

Jung Geun Jang, Daejeon, KR;

Dae Hyun Choo, Daejeon, KR;

Assignee:
Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C07C 5/09 (2006.01); B01J 21/04 (2006.01); B01J 23/745 (2006.01); C01B 3/26 (2006.01); C01B 32/05 (2017.01); C01B 32/162 (2017.01); C01B 32/205 (2017.01); C07C 2/76 (2006.01); C07C 2/78 (2006.01); C07C 2/80 (2006.01); C07C 2/84 (2006.01); C07C 7/09 (2006.01); C09C 1/48 (2006.01);
U.S. Cl.
CPC ...
C07C 5/09 (2013.01); B01J 21/04 (2013.01); B01J 23/745 (2013.01); C01B 3/26 (2013.01); C01B 32/05 (2017.08); C01B 32/162 (2017.08); C01B 32/205 (2017.08); C07C 2/78 (2013.01); C07C 2/80 (2013.01); C07C 2/84 (2013.01); C07C 7/09 (2013.01); C09C 1/48 (2013.01); C01B 2203/0277 (2013.01); C01B 2203/062 (2013.01); C01B 2203/1047 (2013.01); C01P 2006/80 (2013.01); C07C 2521/04 (2013.01); C07C 2523/745 (2013.01);
Abstract

Disclosed is a method for producing hydrogen, carbon, and ethylene from a methane-containing feedstock even without recycling of unreacted methane by providing a single process or system in which a methane-containing feedstock is subjected to two methane conversion steps. The method includes a first conversion step of producing hydrogen and carbonaceous materials and a second conversion step of producing acetylene from unreacted methane and hydrogen discharged from the first conversion step while maintaining a good methane conversion and suppressing coke formation, followed by separating and recovering ethylene and hydrogen produced through selective hydrogenation of acetylene.


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