Solid oxide fuel cell(SOFC) for coproducing syngas and electricity by the internal reforming of carbon dioxide by hydrocarbons and electrochemical membrane reactor system
The present invention relates to a solid oxide fuel cell for internal reforming of hydrocarbons and carbon dioxide, in particular, to a solid oxide fuel cell in which one side of solid oxide electrolyte (YSZ) is attached to an air electrode (La 0.8 Sr 0.2 MnO 3 ) and its other side is attached to a catalyst electrode of Ni-YSZ type or perovskite type metal oxide. The electrochemical conversion system using the solid oxide fuel cell permits the occurrence of internal reforming of hydrocarbons and carbon dioxide concomitantly with the coproduction of a syngas and electricity, and overcomes the shortcomings associated with the catalytic deactivation due to carbon deposition and the high-energy consumption.
1. A solid oxide fuel cell for coproducing syngas and electricity by internal reforming of methane and carbon dioxide, comprising
an ion conductive solid oxide electrolyte,
a catalyst electrode (anode) and an air electrode (cathode) contacting the electrolyte, wherein said catalyst electrode (anode) comprises Ni-YSZ type or perovskite type metal oxide, and
a gas mixture having the following gas volume ratio:
CH 4 :CO 2 :H 2 O:O 2 :H 2 :CO=1:0.4-0.6:0.4-0.7:0.01-0.2:0-1:0-1.
2. The solid oxide fuel cell according to claim 1 , wherein one side of said solid oxide electrolyte is contacts a LaSrMnO 3 type air electrode (cathode) and the other side of said solid oxide electrolyte contacts a catalyst electrode (anode) of Ni-YSZ type or perovskite type metal oxide.
3. The solid oxide fuel cell according to claim 1 or 2 , wherein said Ni-YSZ type metal oxide has a composition of 40-55 wt % of Ni, 40-55 wt % of YSZ and 0-10 wt % of CeO 2 or MgO.
4. An electrochemical conversion system, comprising
a gas feed,
a reactor comprising a solid oxide fuel cell having an air electrode (cathode) and a catalyst electrode (anode) of Ni-YSZ type or perovskite type metal oxide in flow communication with said gas feed,
a gas mixture having the following gas volume ratio:
CH 4 :CO 2 :H 2 O:O 2 :H 2 :CO=1:0.4-0.6:0.4-0.7:0.01-0.2:0-1:0-1,
where the gas mixture is introduced to said reactor through said gas feed.
5. The electrochemical conversion system according to claim 4 , wherein the feed of CO 2 and CH 4 to said system is at least partially from a process producing CO 2 and CH 4 as by-products.