发明名称 Method for producing hydrocarbons from biomass or organic waste
摘要 The present invention relates to a method for producing hydrocarbons from biomass or organic waste. The present invention provides: a method for effectively producing diverse hydrocarbons by using a raw material comprising mixed organic acids that can be obtained by anaerobic fermentation which is a fermentation process in biogasification technology; and a method for producing diverse products such as fuel, lube base oil and aromatics by using a raw material comprising mixed organic acids.
申请公布号 US9187767(B2) 申请公布日期 2015.11.17
申请号 US201113879904 申请日期 2011.10.18
申请人 SK INNOVATION CO., LTD. 发明人 Chung Young Min;Park Cher Hee;Yoon Young Seek;Jeon Hee Jung;Kim Hee Soo;Oh Seung Hoon;Lee Seong Ho;Kim Ok Youn
分类号 C12P5/02;B01J21/06;B01J23/10;B01J23/28;B01J23/34;B01J23/38;B01J23/54;B01J23/883;C07C1/207;B01J23/648;B01J23/882;B01J23/888 主分类号 C12P5/02
代理机构 Abelman, Frayne & Schwab 代理人 Abelman, Frayne & Schwab
主权项 1. A method of producing hydrocarbons, comprising: (a) subjecting biomass or organic waste to anaerobic fermentation to prepare an aqueous organic acid mixture; (b) subjecting the aqueous organic acid mixture to ketonization using a catalyst to prepare an aqueous ketone mixture; (c) subjecting the aqueous ketone mixture to aldol condensation and hydrogenation/hydrodeoxygenation to convert the ketone mixture into the hydrocarbons in the presence of combined catalysts comprising a catalyst having consisting of an aldol condensation catalyst and a hydrogenation/hydrodeoxygenation catalyst under a hydrogen atmosphere in a single reactor, the hydrocarbons selected from the group consisting of fuel, lube base oil, and aromatics; and (d) separating the resulting mixture of hydrocarbons and water obtained in step (c) into the hydrocarbons as an organic phase and the water as an aqueous phase via phase separation, followed by recovering the hydrocarbons, wherein steps (b) and (c), respectively, are performed in presence of water, wherein the aqueous ketone mixture of step (b) is used as it is without removing water therefrom in step (c), wherein the aldol condensation catalyst is selected from the group consisting of CeZrOx, CuZrOx, niobium oxide, zirconia, titania, and oxide mixtures thereof, wherein the hydrogenation/hydrodeoxygenation catalyst is selected from the group consisting of Pd, Pt, Rh, Ru, Ni, NiMo, CoMo, NiW, CoW, and mixtures thereof; wherein the catalyst used in step (b) includes a material selected from the group consisting of MnO, CeO2, ZnO, CaO, MgO, ZrO2, BeO, SrO, BaO, K2O, Rb2O, Cs2O, Na2O, Li2O, and oxide mixtures thereof, and wherein step (c) is performed in the presence of a single catalyst system having the aldol condensation catalyst and the hydrogenation/hydrodeoxygenation catalyst, formed by physical mixing, molding using a binder material or double layering.
地址 Seoul KR