Fuel cell systems and methods

Patent metadata

Field	Value
Publication number	US-12003007-B2
Application number	US-202017781341-A
Country	US
Kind code	B2
Filing date	Nov 25, 2020
Priority date	Dec 3, 2019
Publication date	Jun 4, 2024
Grant date	Jun 4, 2024

Abstract

A fuel cell system comprising (i) at least one fuel cell stack (30) comprising at least one intermediate-temperature solid oxide fuel cell, and having an anode inlet (41) and a cathode inlet (61) and (ii) a reformer (70) for reforming a hydrocarbon fuel to a reformate, and a reformer heat exchanger (160); and defining: an anode inlet gas fluid flow path from a fuel source (90) to said reformer (70) to said fuel cell stack anode inlet (41); a cathode inlet gas fluid flow path from an oxidant inlet (140, 140′, 140″) through at least one cathode inlet gas heat exchanger (110, 150) to said reformer heat exchanger (160) to said fuel cell stack cathode inlet (61); wherein said at least one cathode inlet gas heat exchanger (110, 150) is arranged to heat relatively low temperature cathode inlet gas by transfer of heat from at least one of (i) an anode off-gas fluid flow path and (ii) a cathode off-gas fluid flow path; wherein said reformer heat exchanger is arranged for heating said anode inlet gas from said relatively high temperature cathode inlet gas to a temperature T3 at the anode inlet that is below a temperature T1 at the cathode inlet; and wherein oxidant flow control means (200) for controlled mixing of low temperature oxidant from the or each oxidant inlet (140, 140′, 140″) with high temperature cathode inlet gas to control a temperature T1 at the cathode inlet (61) relative to a temperature T3 at the anode inlet (41) and at a level higher than T3.

First claim

The invention claimed is:

1. A fuel cell system comprising:
(i) at least one fuel cell stack comprising at least one intermediate-temperature solid oxide fuel cell, and having an anode inlet, a cathode inlet, an anode off-gas outlet, and a cathode off-gas outlet; and
(ii) a reformer for reforming a hydrocarbon fuel to a reformate, and having a reformer inlet for anode inlet gas, a reformer outlet for exhausting anode inlet gas, and a reformer heat exchanger;
(iii) a controller;
and defining:
(a) an anode inlet gas fluid flow path from a fuel source to said reformer to said at least one fuel cell stack anode inlet;
(b) an anode off-gas fluid flow path from said at least one fuel cell stack anode off-gas outlet to a fuel cell system exhaust;
(c) a cathode inlet gas fluid flow path from an at least one oxidant inlet through at least one cathode inlet gas heat exchanger to said reformer heat exchanger to said at least one fuel cell stack cathode inlet;
(d) a cathode off-gas fluid flow path from said at least one fuel cell stack cathode off-gas outlet to said fuel cell system exhaust; and
wherein said at least one cathode inlet gas heat exchanger is configured to heat relatively low temperature cathode inlet gas by the transfer of heat from at least one of (i) said anode off-gas fluid flow path, and (ii) said cathode off-gas fluid flow path, to provide relatively high temperature cathode inlet gas;

characterized in that said reformer heat exchanger is configured to heat said anode inlet gas from said relatively high temperature cathode inlet gas to a temperature T 3 at the anode inlet that is below a temperature T 1 at the cathode inlet; and further characterized by said controller controlling mixing of low temperature oxidant from the at least one oxidant inlet or each oxidant inlet with high temperature cathode inlet gas to control a temperature T 1 at the cathode inlet relative to a temperature T 3 at the anode inlet and at a level higher than T 3 .

2. The system according to claim 1 , wherein the controller is arranged to control mixing of low temperature oxidant from an oxidant inlet at the cathode inlet so as to reduce the temperature T 1 .

3. The system according to claim 1 , wherein the controller is arranged to control mixing of low temperature oxidant from an oxidant inlet at an input to the reformer heat exchanger so as to reduce the temperature T 1 while also reducing the temperature T 3 .

4. The system according to claim 1 , wherein the reformer heat exchanger comprises a hot bypass for cathode inlet gas to bypass the reformer heat exchanger and contribute to elevating said cathode inlet gas to temperature T 1 at the cathode inlet.

5. The system according to claim 4 , wherein the hot bypass comprises a pre-set aperture restrictor.

6. The system according to claim 4 , wherein the hot bypass cathode inlet gas is drawn from the cathode inlet gas fluid flow path prior to mixing of low temperature oxidant.

7. The system according to claim 4 , wherein the hot bypass comprises a controllable restrictor.

8. The system according to claim 1 , wherein the oxidant flow control means is arranged to derive a reformer bypass air flow demand output signal from a reformer temperature input, which indicates fuel temperature at the reformer outlet, and a reformer setpoint input.

9. The system according to claim 8 further comprising a tail-gas burner in fluid flow communication with said at least one fuel cell stack anode and cathode off-gas outlets, having a tail-gas burner exhaust, defining a fluid flow path from said at least one fuel cell stack anode and cathode off-gas outlets to said tail-gas burner exhaust to said exhaust and further comprising a tail-gas burner exhaust temperature sensor for sensing a tail-gas burner exhaust temperature (T TGB ), wherein said controller is further arranged to derive a tail gas burner exhaust temperature setpoint from the reformer temperature input and the reformer setpoint input.

10. The system according to claim 9 further comprising tail gas burner control means for providing a fuel demand actuator command derived from the tail gas burner exhaust temperature setpoint and the tail-gas burner exhaust temperature so as to increase supply of fuel to the tail gas burner when the tail-gas burner exhaust temperature is below the tail gas burner exhaust temperature setpoint as provided by the controller.

11. The system according to claim 1 , comprising first and second oxidant mixers, the first mixer arranged for mixing low temperature oxidant from an oxidant inlet at an inlet to the reformer heat exchanger and the second mixer arranged for mixing low temperature oxidant from an oxidant inlet at a reformer heat exchanger outlet and cathode inlet.

12. The system according to claim 1 , wherein the cathode inlet gas fluid flow path has a temperature of 750-850 degrees centigrade at its hottest point in steady state operation at ambient temperature air input.

13. The system according to claim 1 , wherein T 1 is controlled to be between 50 and 150 degrees centigrade higher than T 3 in steady state operation at ambient temperature air input.

14. The system according to claim 1 , wherein T 1 is controlled to be between 500 and 600 degrees centigrade in steady state operation at ambient temperature air input.

15. The system according to claim 1 , wherein T 3 is controlled to be between 400 and 500 degrees centigrade in steady state operation at ambient temperature air input.

16. The system according to claim 1 , wherein the reformer heat exchanger is a co-flow or parallel heat exchanger.

17. A method of operating a fuel cell having:
(i) at least one fuel cell stack comprising at least one intermediate-temperature solid oxide fuel cell, and having an anode inlet, a cathode inlet, an anode off-gas outlet, and a cathode off-gas outlet; and
(ii) a reformer for reforming a hydrocarbon fuel to a reformate, and having a reformer inlet for anode inlet gas, a reformer outlet for exhausting anode inlet gas, and a reformer heat exchanger;
(iii) a controller
and defining:
(a) an anode inlet gas fluid flow path from a fuel source to said reformer to said at least one fuel cell stack anode inlet;
(b) an anode off-gas fluid flow path from said at least one fuel cell stack anode off-gas outlet to a fuel cell system exhaust;
(c) a cathode inlet gas fluid flow path from an at least one oxidant inlet through at least one cathode inlet gas heat exchanger to said reformer heat exchanger to said at least one fuel cell stack cathode inlet; and
(d) a cathode off-gas fluid flow path from said at least one fuel cell stack cathode off-gas outlet to said fuel cell system exhaust; the method comprising:
heating relatively low temperature cathode inlet gas by heat exchange from at least one of (i) said anode off-gas fluid flow path and (ii) said cathode off-gas fluid flow path, to provide relatively high temperature cathode inlet gas;
heating said anode inlet gas from said relatively high temperature cathode inlet gas to a temperature T 3 at the anode inlet that is below a temperature T 1 at the cathode inlet; and
using the controller, mixing of low temperature oxidant from the or each oxidant inlet with high temperature cathode inlet gas to control, at a level higher than T 3 , the temperature T 1 at the cathode inlet.

18. A fuel cell system comprising:
(i) at least one fuel cell stack comprising at least one intermediate-temperature solid oxide fuel cell, and having an anode inlet, a cathode inlet, an anode off-gas outlet, and a cathode

Assignees

• Ceres Ip Co Ltd

Inventors

• Postlethwaite Oliver John
• Dozio Simone Stefano
• Bertoni Simone
• Barnard Paul Adrian

Classifications

• H01M8/0618 Primary

  Reforming processes, e.g. autothermal, partial oxidation or steam reforming · CPC title

• H01M8/04014 Primary

  Heat exchange using gaseous fluids; Heat exchange by combustion of reactants · CPC title

• H01M8/04022

  Heating by combustion · CPC title

• H01M8/04328

  of anode reactants at the inlet or inside the fuel cell · CPC title

• H01M8/04335

  of cathode reactants at the inlet or inside the fuel cell · CPC title