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公开(公告)号:US10418657B2
公开(公告)日:2019-09-17
申请号:US14506743
申请日:2014-10-06
Applicant: PHILLIPS 66 COMPANY
Inventor: Ying Liu , Mingfei Liu , David M. Bierschenk , Ting He
IPC: H01M8/1246 , H01M8/1253 , H01M8/126 , H01M8/1213 , H01M4/86 , H01M4/88 , H01M4/90 , H01M8/124
Abstract: The present embodiment describes a method of forming different layers in a solid oxide fuel cell. The method begins by preparing slurries which are then delivered to a spray nozzle. The slurries are then atomized and sprayed subsequently onto a support to produce a layer which is then dried. In this embodiment different layers can comprise an anode, an electrolyte and a cathode. Also the support can be a metal or a metal oxide which is later removed.
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公开(公告)号:US20180287178A1
公开(公告)日:2018-10-04
申请号:US15935460
申请日:2018-03-26
Applicant: Phillips 66 Company
Inventor: Mingfei Liu , Ying Liu
IPC: H01M8/1226 , H01M8/1253 , H01M8/126 , H01M4/88
Abstract: A process for producing a solid oxide reactor. The process begins by separately preparing an anode slurry and an electrolyte slurry. The electrolyte slurry is then tape casted onto a support layer to produce an electrolyte layer situated above the support layer. The anode slurry is then tape casted onto the electrolyte layer to produce a first multilayer structure comprising an anode layer situated above the electrolyte layer situated above the support layer. The support layer is then removed from the first multilayer structure to produce a second multilayer structure comprising the anode layer situated above the electrolyte layer. The second multilayer structure is then sintered to produce a solid oxide reactor.
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公开(公告)号:US20160329576A1
公开(公告)日:2016-11-10
申请号:US15096901
申请日:2016-04-12
Applicant: Phillips 66 Company
Inventor: Mingfei Liu , Ting He , Ying Liu , David M. Bierschenk , Michael Keane
IPC: H01M8/0243 , H01M8/1226 , H01M8/1253 , H01M8/126 , H01M4/88 , H01M4/86
CPC classification number: H01M8/1226 , H01M4/8803 , H01M4/8846 , H01M4/9025 , H01M2008/1293
Abstract: A solid oxide fuel cell comprising a cathode, an electrolyte, a functional layer and an anode support. The anode support comprises A-B-C: A is a nitrate, an oxide, a salt or a carbonate selected from the group of: alkali, alkaline oxide, alkaline earth metal or combinations thereof, B is selected from the group of: Fe, Ni, Cu, Co or combinations thereof, and C is selected from the group of: PSZ, YSZ, SSZ, SDC, Ce doped SSZ, GDC or combinations thereof. In the solid oxide fuel cell A ranges from about 0 to about 20 wt % of the anode support, B ranges from about 0.1 to about 70 wt % of the anode support and C ranges from about 0.1 to about 60 wt % of the anode support.
Abstract translation: 一种固体氧化物燃料电池,包括阴极,电解质,功能层和阳极支撑体。 阳极载体包括ABC:A是选自碱金属,碱土金属,碱土金属或其组合的硝酸盐,氧化物,盐或碳酸盐,B选自Fe,Ni,Cu ,Co或其组合,C选自:PSZ,YSZ,SSZ,SDC,Ce掺杂的SSZ,GDC或其组合。 在固体氧化物燃料电池A的范围为阳极支撑体的约0至约20重量%的范围内,B为阳极支撑体的约0.1至约70重量%,C为阳极支撑体的约0.1至约60重量% 。
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公开(公告)号:US20150099212A1
公开(公告)日:2015-04-09
申请号:US14504774
申请日:2014-10-02
Applicant: PHILLIPS 66 COMPANY
Inventor: David M. Bierschenk , Ying Liu , Mingfei Liu , Ting He
CPC classification number: H01M8/1213 , H01M4/8621 , H01M4/8652 , H01M4/8657 , H01M4/8817 , H01M4/8867 , H01M4/8878 , H01M4/9025 , H01M4/9033 , H01M4/905 , H01M4/9058 , H01M8/1246 , H01M2008/1293 , H01M2300/0074 , H01M2300/0077 , Y02E60/525 , Y02P70/56
Abstract: A solid oxide fuel cell comprising an electrolyte, an anode and a cathode. In this fuel cell at least one electrode has been modified with a promoter using gas phase infiltration.
Abstract translation: 一种固体氧化物燃料电池,包括电解质,阳极和阴极。 在该燃料电池中,使用气相渗透的助催化剂修饰了至少一个电极。
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公开(公告)号:US20150099209A1
公开(公告)日:2015-04-09
申请号:US14506743
申请日:2014-10-06
Applicant: PHILLIPS 66 COMPANY
Inventor: Ying Liu , Mingfei Liu , David M. Bierschenk , Ting He
IPC: H01M8/12
CPC classification number: H01M8/1246 , H01M4/8621 , H01M4/886 , H01M4/9025 , H01M8/1213 , H01M8/1253 , H01M8/126 , H01M2008/1293 , H01M2300/0074 , H01M2300/0077 , Y02E60/525 , Y02P70/56
Abstract: The present embodiment describes a method of forming different layers in a solid oxide fuel cell. The method begins by preparing slurries which are then delivered to a spray nozzle. The slurries are then atomized and sprayed subsequently onto a support to produce a layer which is then dried. In this embodiment different layers can comprise an anode, an electrode and a cathode. Also the support can be a metal or a metal oxide which is later removed.
Abstract translation: 本实施例描述了在固体氧化物燃料电池中形成不同层的方法。 该方法开始于制备浆料,然后将其输送到喷嘴。 然后将浆料雾化并随后喷洒到载体上以产生干燥后的层。 在该实施例中,不同的层可以包括阳极,电极和阴极。 此外,载体可以是稍后除去的金属或金属氧化物。
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公开(公告)号:US20220131161A1
公开(公告)日:2022-04-28
申请号:US17449835
申请日:2021-10-04
Applicant: PHILLIPS 66 COMPANY
Inventor: Mingfei Liu , Ying Liu
IPC: H01M8/0236
Abstract: A fuel cell comprising an indium tin oxide cathode contact is in physical contact subjacent an upper interconnect and in physical contact superjacent a cathode. In this fuel cell an electrolyte is in physical contact subjacent a cathode and superjacent an anode. Finally, a lower interconnect is subjacent the anode.
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公开(公告)号:US20220059862A1
公开(公告)日:2022-02-24
申请号:US17394524
申请日:2021-08-05
Applicant: PHILLIPS 66 COMPANY
Inventor: Mingfei Liu , Ying Liu , Mark Jensen
IPC: H01M8/248
Abstract: A system for a solid oxide fuel cell stack disposed between and in contact with a fixed top compression plate and a movable compression plate. At least one tension rod can be inserted through an opening on a movable locking plate, wherein the top end of the tension rod is connected to the bottom of the movable compression plate and the bottom end of the tension rod is connected to a fixed bottom compression plate. At least one nut can be used in conjunction each tension rod and disposed below the movable locking plate to secure the movable locking plate in position. Additionally, at least one spring can be disposed around the at least one tension rod and connected to the bottom of the movable compression plate and the top of the fixed bottom compression plate. Finally, at least one pneumatic cylinder can be in contact with the bottom of the movable locking plate and the fixed bottom compression plate.
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公开(公告)号:US11145870B2
公开(公告)日:2021-10-12
申请号:US16710657
申请日:2019-12-11
Applicant: PHILLIPS 66 COMPANY
Inventor: Ye Lin , Ying Liu , Mingfei Liu
Abstract: A method of producing an infiltrated solid oxide fuel cell (SOFC) layer. The method begins by infiltrating a solution containing a solute into a SOFC layer to produce a primary SOFC layer. The primary SOFC layer is then dried in a heated environment, wherein the heated environment ranges in temperature from about 25° C. to about 100° C. to produce a dry primary SOFC layer. The dry primary SOFC layer is then cooled at a rate less than about 5° C./min to room temperature to produce a cooled primary SOFC layer. The cooled primary SOFC layer is then heated to a temperature greater than 500° C. then quenching to a temperature from about 10° C. to about 30° C. to produce an infiltrated SOFC layer.
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公开(公告)号:US20210249668A1
公开(公告)日:2021-08-12
申请号:US17169750
申请日:2021-02-08
Applicant: PHILLIPS 66 COMPANY
Inventor: Mingfei Liu , Ying Liu , Mark J. Jensen
IPC: H01M8/0273 , H01M8/0282
Abstract: A metal frame for sealing a solid oxide fuel cell. The metal frame comprises both a metal top frame positioned on top of a middle frame and a metal bottom frame that is positioned below a middle frame.
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公开(公告)号:US10326157B2
公开(公告)日:2019-06-18
申请号:US15096901
申请日:2016-04-12
Applicant: Phillips 66 Company
Inventor: Mingfei Liu , Ting He , Ying Liu , David M. Bierschenk , Michael Keane
IPC: H01M8/00 , H01M8/1226 , H01M4/88 , H01M4/90 , H01M8/124
Abstract: A solid oxide fuel cell comprising a cathode, an electrolyte, a functional layer and an anode support. The anode support comprises A-B-C: A is a nitrate, an oxide, a salt or a carbonate selected from the group of: alkali, alkaline oxide, alkaline earth metal or combinations thereof, B is selected from the group of: Fe, Ni, Cu, Co or combinations thereof, and C is selected from the group of: PSZ, YSZ, SSZ, SDC, Ce doped SSZ, GDC or combinations thereof. In the solid oxide fuel cell A ranges from about 0 to about 20 wt % of the anode support, B ranges from about 0.1 to about 70 wt % of the anode support and C ranges from about 0.1 to about 60 wt % of the anode support.
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