IP Library Granted Patent US 10,008,730
Granted Patent B2
US 10,008,730 · App. 14/730,034 · Granted Jun 26, 2018

System and method for fueling alternative fuel vehicles

Inventors: Aqil Jamal (Dhahran, SA); Thang Pham (Dhahran, SA)
Assignee: Saudi Arabian Oil Company
H01M8/0618B60L11/1883B65B1/00C01B3/382C01B3/384C01B3/48C01B3/56F17C5/06H01M8/04201H01M8/0637H01M8/0656H01M8/0662H01M8/12H01M8/1231C01B2203/0233C01B2203/0283C01B2203/043C01B2203/0455C01B2203/0485C01B2203/066C01B2203/0811C01B2203/1258C01B2203/1288C01B2203/141C01B2203/148H01M8/04097H01M8/0668H01M8/0675H01M2008/1293H01M2250/10H01M2250/20H01M2300/0074Y02B90/14Y02E60/321Y02E60/50Y02E60/525Y02T90/32Y02T90/34
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Quick Facts
Patent No.
US 10,008,730
App. No.
14/730,034
Granted
Jun 26, 2018
Kind
B2
Abstract

Disclosed is an alternative fuel fueling station useful for fueling both electrical and hydrogen alternative fuel vehicles simultaneously. The alternative fuel fueling station includes a solid oxide fuel cell, an electrical conduit, and a compressed hydrogen conduit, such that the alternative fuel fueling station can fuel both the electrical and hydrogen alternative fuel vehicles simultaneously.

Claims (15)

1. An alternative fuel fueling station useful for fueling both electrical and hydrogen alternative fuel vehicles simultaneously, the alternative fuel fueling station comprising:

a solid oxide fuel cell (“SOFC”) system comprising a solid oxide fuel cell;

an electrical conduit that is operable to electrically couple an alternative fuel storage device of the electrical alternative fuel vehicle to the solid oxide fuel cell of the SOFC system and to convey electrical current produced by the SOFC system to the electrical alternative fuel vehicle;

a hydrogen compression and storage system; and

a compressed hydrogen conduit that is operable to both fluidly couple an alternative fuel storage device of the hydrogen alternative fuel vehicle to the hydrogen compression and storage system of the SOFC system and convey compressed hydrogen having a pressure in a range of from about 350 bars to about 700 bars and having a hydrogen mole purity of about 99.99 percent to the hydrogen alternative fuel vehicle,

where the alternative fuel fueling station can fuel both the electrical and hydrogen alternative fuel vehicles simultaneously,

where the SOFC system includes a hydrodesulfurization system that fluidly couples to the hydrogen compression and storage system and is operable to receive a hydrocarbon fuel;

the alternative fuel fueling station further comprising an oxygen generation system, a hydrogen purification system, an anode side of the solid oxide fuel cell with an outlet, and a steam reformer having catalytic reactor tubes and a reformer combustion chamber, where the catalytic reactor tubes couple to the hydrodesulfurization system and are operable to receive steam, and where the reformer combustion chamber thermally couples to the catalytic reactor tubes and fluidly couples to both the outlet of the anode side of the solid oxide fuel cell and the oxygen generation system and is operable to receive the hydrocarbon fuel,

the anode side operable to receive a methane-rich anode feed gas without a reformer, the methane-rich anode feed gas comprising a pre-reformer syngas product and an off-gas stream from the hydrogen purification system, where the off-gas stream comprises methane, carbon oxides, and inert gases, where the methane-rich anode feed gas comprises methane, carbon oxides, hydrogen, and water,

the anode side further operable to reform, by a reforming catalyst in the solid oxide fuel cell, and electrochemically convert methane and water contained in the methane-rich anode feed gas into hydrogen and carbon oxides to generate electrical power,

where the hydrogen purification system fluidly couples to the catalytic reactor tubes and is operable to produce a purified hydrogen gas,

where the hydrogen compression and storage system is fluidly coupled to the hydrogen purification system and is operable to produce the compressed hydrogen, and

the alternative fuel fueling station further comprising a pre-reformer that fluidly couples to the outlet of the anode side of the solid oxide fuel cell and is operable to receive the hydrocarbon fuel and to produce the pre-reformer syngas product, where the anode side of the solid oxide fuel cell has an inlet that fluidly couples to both the pre-reformer and the hydrogen purification system and is operable to produce an anode exhaust gas.

2. The alternative fuel fueling station of claim 1 , where the oxygen generation system is operable to produce oxygen.

3. The alternative fuel fueling station of claim 2 , further comprising a CO2 purification and liquidification system that fluidly couples to the reformer combustion chamber and is operable to produce a refined carbon dioxide product.

Assignments (2)
CORRECTIVE ASSIGNMENT TO CORRECT THE DOCKET NUMBER 004159.005388 (SA5388) PREVIOUSLY RECORDED ON REEL 035789 FRAME 0248. ASSIGNOR(S) HEREBY CONFIRMS THE DOCKET NUMBER 004159.005388 (SA5388). Recorded Jul 7, 2015
From: JAMAL, AQIL; PHAM, THANG
To: SAUDI ARABIAN OIL COMPANY
Reel/Frame 036066/0048 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 4, 2015
From: JAMAL, AQIL; PHAM, THANG
To: SAUDI ARABIAN OIL COMPANY
Reel/Frame 035789/0248 →
Continuity (3)
Division 13683272 · Nov 21, 2012
Provisional Application 61562189 · Nov 21, 2011
Related Publication 20150266393A1 · Sep 24, 2015
Cited By (10)
US 12,191,543 US 12,240,758 US 12,258,272 US 12,288,908 US 12,358,792 US 12,358,793 US 12,358,794 US 12,459,813 US 12,565,423 US 12,725,857