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公开(公告)号:US20230331644A1
公开(公告)日:2023-10-19
申请号:US18025372
申请日:2021-08-10
Inventor: Yong Tae KIM , Sung Woo LEE , Seok Ki KIM , Jungho SHIN , Seung Ju HAN , Hyun Woo KIM , Eun Hae SIM
IPC: C07C2/76
CPC classification number: C07C2/76 , C07C2523/755 , C07C2523/26 , C07C2521/18
Abstract: The present disclosure relates to a method for non-oxidative direct conversion of methane. Specifically, in the method, a methane/hydrogen gas is introduced into an Inconel 600 reactor at a superficial velocity of 100 to 200 cm·min−1 and a catalyst is not externally introduced into the reactor. Under the conditions, a non-oxidative direct methane conversion reaction is performed in the Inconel 600 reactor. The method maximizes the reaction rate, minimizes coke formation, and increases the yields of C2 hydrocarbon compounds and aromatic compounds.
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公开(公告)号:US20250018357A1
公开(公告)日:2025-01-16
申请号:US18687504
申请日:2022-08-02
Inventor: Yong Tae KIM , Sung Woo LEE , Jungho SHIN , Seung Ju HAN , Tsegay Gebrekidan GEBREYOHANNES
Abstract: The present invention relates to a nonoxidative methane direct converting reactor and a preparation method of ethylene and aromatic compound using the same and, more specifically, to a nonoxidative methane direct converting reactor and a preparation method of ethylene and aromatic compound using the same, wherein the reactor maximizes a catalytic reaction rate, minimizes cokes production, and provides a high conversion rate of methane and a high yield of ethylene and an aromatic compound even at a low hydrogen supply ratio in the production of ethylene and an aromatic compound from methane.
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公开(公告)号:US20220339605A1
公开(公告)日:2022-10-27
申请号:US17763555
申请日:2020-09-03
Inventor: Yong Tae KIM , Sung Woo LEE , Seung Ju HAN , Seok Ki KIM , Hyun Woo KIM , Jungho SHIN
Abstract: The present invention relates to a catalyst for selective hydrogenation of acetylene and a preparation method thereof. More specifically, the catalyst and preparation method maximize the catalytic reaction rate at various reaction temperatures and suppress side reactions to minimize the generation of green oil and cokes and to improve the deactivation rate of a catalyst when preparing ethylene from acetylene. Thus, the catalyst and the preparation method provide a high conversion rate of acetylene and a high ethylene production yield.
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