US 12,102,974 B2
Reactor for the conversion of carbon dioxide
Vincent Piepiora, Versailles (FR); Stéphanie Ognier, Paris (FR); Simeon Cavadias, Rueil Malmaison (FR); Xavier Duten, Fontenay-sous-Bois (FR); Michael Tatoulian, Paris (FR); Maria Elena Galvez-Parruca, Pantin (FR); and Patrick Da Costa, Pantin (FR)
Assigned to Paris Sciences et Lettres, (FR); Centre National de la Recherche Scientifique (CNRS), (FR); Sorbonne Universite, (FR); Ecole Nationale Superieure de Chimie de Paris, (FR); and Univ Paris XIII Paris-Nord Villetaneuse, (FR)
Appl. No. 17/416,225
Filed by Paris Sciences et Lettres, Paris (FR); Centre National de la Recherche Scientifique (CNRS), Paris (FR); Sorbonne Universite, Paris (FR); Ecole Nationale Superieure de Chimie de Paris, Paris (FR); and Univ Paris XIII Paris-Nord Villetaneuse, Villetaneuse (FR)
PCT Filed Dec. 20, 2019, PCT No. PCT/EP2019/086743
§ 371(c)(1), (2) Date Jun. 18, 2021,
PCT Pub. No. WO2020/128009, PCT Pub. Date Jun. 25, 2020.
Claims priority of application No. 1874033 (FR), filed on Dec. 21, 2018.
Prior Publication US 2022/0040664 A1, Feb. 10, 2022
Int. Cl. B01J 19/08 (2006.01); B01J 8/06 (2006.01); B01J 19/24 (2006.01); B01J 23/755 (2006.01); C07C 1/04 (2006.01); C07C 1/12 (2006.01); C07C 29/152 (2006.01); C07C 29/156 (2006.01); H05H 1/24 (2006.01)
CPC B01J 19/088 (2013.01) [B01J 8/06 (2013.01); B01J 19/242 (2013.01); B01J 23/755 (2013.01); C07C 1/041 (2013.01); C07C 1/12 (2013.01); C07C 29/152 (2013.01); C07C 29/156 (2013.01); H05H 1/2406 (2013.01); H05H 1/2431 (2021.05); H05H 1/245 (2021.05); B01J 2219/0809 (2013.01); B01J 2219/0815 (2013.01); B01J 2219/0828 (2013.01); B01J 2219/083 (2013.01); B01J 2219/0841 (2013.01); B01J 2219/0849 (2013.01); B01J 2219/0871 (2013.01); B01J 2219/0875 (2013.01); B01J 2219/0892 (2013.01); B01J 2219/0896 (2013.01); B01J 2219/182 (2013.01); B01J 2219/1943 (2013.01); B01J 2219/2408 (2013.01); B01J 2219/2411 (2013.01); B01J 2219/243 (2013.01); C07C 2523/755 (2013.01); H05H 2245/15 (2021.05)] 19 Claims
OG exemplary drawing
 
1. A reactor for conversion of carbon dioxide or carbon monoxide into hydrocarbon and/or alcohol, comprising:
a support made of an electrically and thermally conductive material, the support forming a wall of a longitudinal channel, the longitudinal channel passing through the support, the support acting as a cathode of the reactor,
a wire electrode forming an anode of the reactor, the wire electrode comprising a part that extends within the longitudinal channel along the longitudinal channel, the part being arranged at a distance from the wall of the longitudinal channel, the part being optionally covered by an electrically insulating layer,
a catalyst configured to catalyse a conversion reaction of carbon dioxide or carbon monoxide into hydrocarbon and/or alcohol, the catalyst being located between the wire electrode and the wall of the longitudinal channel,
wherein the longitudinal channel is a plurality of longitudinal channels, the plurality of longitudinal channels being arranged according to a bidimensional network according to a plane of the network, the plurality of longitudinal channels being parallel to each other and perpendicular to a plane of the network.