Fuel cell system including high-temperature desulfurization subsystem and method of operating the same

Patent metadata

Field	Value
Publication number	US-10847824-B2
Application number	US-201816130547-A
Country	US
Kind code	B2
Filing date	Sep 13, 2018
Priority date	Sep 13, 2018
Publication date	Nov 24, 2020
Grant date	Nov 24, 2020

Abstract

A fuel cell system includes a hot box, a stack of fuel cells disposed in the hot box, and a desulfurization subsystem. The desulfurization subsystem may include a sulfur adsorption reactor containing a metal oxide, such as ZnO, configured to adsorb sulfur species from fuel, a first fuel conduit configured to provide fuel to the reactor, and a second fuel conduit configured to receive fuel from the reactor. The desulfurization subsystem may be configured to heat the reactor to an operating temperature ranging from about 200° C. to about 450° C., using heat generated in the hot box.

First claim

What is claimed is:

1. A fuel cell system comprising:
a hot box;
a stack of fuel cells disposed in the hot box; and
a desulfurization subsystem comprising:
a sulfur adsorption reactor comprising a metal oxide configured to adsorb sulfur species from fuel; and
a first fuel conduit configured to provide fuel to the reactor,
wherein the subsystem is configured to heat the reactor to an operating temperature ranging from about 200° C. to about 450° C., using heat generated in the hot box;

wherein the subsystem further comprises:
a cathode exhaust conduit configured to receive at least one of cathode exhaust or anode tail gas oxidizer (ATO) exhaust from the hot box; and
a cathode heat exchanger configured to transfer heat from the at least one of the cathode exhaust or the ATO exhaust in the cathode exhaust conduit to fuel in the first fuel conduit.

2. The system of claim 1 , wherein the subsystem further comprises a fuel heat exchanger configured to transfer heat from fuel in a second fuel conduit to fuel in the first fuel conduit.

3. The system of claim 2 , wherein the subsystem further comprises a trim heater configured to heat fuel in the first fuel conduit.

4. The system of claim 3 , wherein the cathode heat exchanger is disposed upstream of the fuel heat exchanger, and the fuel heat exchanger is disposed upstream of the trim heater, with respect to a fuel flow direction through the first fuel conduit to the reactor.

5. The system of claim 1 , wherein the subsystem further comprises:
an anode exhaust conduit configured to provide anode exhaust from the hot box to the cathode exhaust conduit; and
an oxidation catalyst configured to catalyze oxidation of a mixture of anode exhaust and cathode exhaust in the cathode exhaust conduit.

6. The system of claim 1 , wherein the subsystem further comprises:
a bypass conduit; and
a splitter configured to divert a portion of cathode exhaust or the ATO exhaust in the cathode exhaust conduit into the bypass conduit.

7. The system of claim 1 , wherein the subsystem further comprises a cathode blower configured to pull cathode exhaust or ATO exhaust from the hot box through the cathode exhaust conduit.

8. A fuel cell system comprising:
a hot box;
a stack of fuel cells disposed in the hot box; and
a desulfurization subsystem comprising:
a sulfur adsorption reactor comprising a metal oxide configured to adsorb sulfur species from fuel; and
a first fuel conduit configured to provide fuel to the reactor,
wherein the subsystem is configured to heat the reactor to an operating temperature ranging from about 200° C. to about 450° C., using heat generated in the hot box;

wherein the subsystem further comprises:
an anode exhaust conduit configured to receive anode exhaust from the hot box; and
an anode heat exchanger configured to transfer heat from anode exhaust in the anode exhaust conduit to fuel in the first fuel conduit;
wherein the subsystem further comprises a trim heater configured to heat fuel in the first fuel conduit, wherein the trim heater is disposed downstream of the anode heat exchanger, with respect to a fuel flow direction through the first fuel conduit to the reactor.

9. A fuel cell system comprising:
a hot box;
a stack of fuel cells disposed in the hot box; and
a desulfurization subsystem comprising:
a sulfur adsorption reactor comprising a metal oxide configured to adsorb sulfur species from fuel; and
a first fuel conduit configured to provide fuel to the reactor,
wherein the subsystem is configured to heat the reactor to an operating temperature ranging from about 200° C. to about 450° C., using heat generated in the hot box;

wherein the subsystem further comprises:
an air conduit thermally connected to the hot box, such that air in the air conduit is heated by heat generated in the hot box;
an air heat exchanger configured to transfer heat from air in the air conduit to fuel in the first fuel conduit; and
a blower configured to force air through the air conduit.

10. The system of claim 9 , wherein the air conduit is disposed between the hot box and an insulation layer covering the hot box.

11. A fuel cell system comprising:
a hot box;
a stack of fuel cells disposed in the hot box; and
a desulfurization subsystem comprising:
a sulfur adsorption reactor comprising a metal oxide configured to adsorb sulfur species from fuel; and
a first fuel conduit configured to provide fuel to the reactor,
wherein the subsystem is configured to heat the reactor to an operating temperature ranging from about 200° C. to about 450° C., using heat generated in the hot box;

wherein the first fuel conduit is disposed between the hot box and an insulation layer covering the hot box, such that fuel in the first fuel conduit is heated by heat generated in the hot box.

12. The system of claim 11 , wherein the reactor is disposed between the hot box and an insulation layer covering the hot box, such that the reactor is heated by heat generated in the hot box.

13. A fuel cell system comprising:
a hot box;
a stack of fuel cells disposed in the hot box; and
a desulfurization subsystem comprising:
a sulfur adsorption reactor comprising a metal oxide configured to adsorb sulfur species from fuel; and
a first fuel conduit configured to provide fuel to the reactor,
wherein the subsystem is configured to heat the reactor to an operating temperature ranging from about 200° C. to about 450° C., using heat generated in the hot box;

wherein:
the reactor comprises an adsorption bed comprising ZnO; and
the system further comprises a catalytic partial oxidation (CPOx) reactor configured to provide fuel to the first fuel conduit during steady-state system operation, and to provide only air to the first conduit after system shutdown to regenerate the ZnO adsorption bed.

14. A fuel cell system comprising:
a hot box;
a stack of fuel cells disposed in the hot box; and
a desulfurization subsystem comprising:
a sulfur adsorption reactor comprising a metal oxide configured to adsorb sulfur species from fuel; and
a first fuel conduit configured to provide fuel to the reactor,
wherein the subsystem is configured to heat the reactor to an operating temperature ranging from about 200° C. to about 450° C., using heat generated in the hot box;

wherein the reactor comprises:
first and second adsorption beds comprising ZnO;
a fuel valve configured to selectively direct fuel from the first fuel conduit into one of the first and second adsorption beds; and
an air valve configured to selectively direct air from an air conduit into one of the first and second adsorption beds, wherein the fuel and air valves are configured such that air and fuel is not directed into the same adsorption bed;
wherein:
the system comprises a catalytic partial oxidation (CPOx) reactor configured to provide fuel to the first fuel conduit;
the CPOx reactor comprises a blower configured to provide air to the air conduit; and
the reactor comprises a heater configured to heat air in the air conduit.

Assignees

• Bloom Energy Corp

Inventors

• Weingaertner David
• El Batawi Emad

Classifications

• H01M2008/1293

  Fuel cells with solid oxide electrolytes · CPC title

• H01M8/0675 Primary

  Removal of sulfur · CPC title

• H01M8/0662

  Treatment of gaseous reactants or gaseous residues, e.g. cleaning · CPC title

• H01M8/04089

  of gaseous reactants · CPC title

• H01M8/04067

  Heat exchange or temperature measuring elements, thermal insulation, e.g. heat pipes, heat pumps, fins · CPC title