DEVICE FOR DETERMINING THE HYDROGEN CONCENTRATION OF AN EXHAUST GAS IN AN EXHAUST GAS LINE OF A FUEL CELL SYSTEM, AND FUEL CELL SYSTEM

Abstract

The invention relates to a device (1) for determining the H2 concentration of a fluid in an exhaust gas line (12) of a fuel cell system (100), comprising a sensor (14) which is arranged in a pipe section (2), said pipe section having an inflow opening (4) and an outflow opening (6). An installation element (8) divides exhaust gas arriving through the inflow opening (4) into a first volumetric flow which flows through a first pipe volume (V1) and at least one additional volumetric flow which flows through at least one additional pipe volume (V2). A purge line (41) opens into the first pipe volume (V1) between the inflow opening (4) and the H2 sensor (14). The sensor (14) measures the H2 concentration of the exhaust gas in the first pipe volume (V1).

Claims

1. A device (1) for determining the hydrogen concentration of an exhaust gas in an exhaust gas line (12) of a fuel cell system (100), comprising a sensor (14), which is disposed in a pipe section (2), wherein the pipe section (2) comprises an inflow opening (4) and an outflow opening (6), wherein an installation element (8) divides an exhaust gas which has passed through the inflow opening (4) into a first volumetric flow which flows through a first pipe volume (V1) and at least one further volumetric flow which flows through at least one further pipe volume (V2), wherein the sensor (14) measures the hydrogen concentration of the exhaust gas in the first pipe volume (V1).

2. The device according to claim 1, wherein the pipe section (2) comprises a connector (41) for a purge line (40), wherein a purge gas from the purge line (40) is fed into the first volume (V1) via the connector (41).

3. The device (1) according to claim 2, wherein in the connector (41) for the purge line (40) is disposed between the inflow opening (4) and the sensor (14).

4. The device (1) according to claim 3, wherein a swirl element is disposed between the connector (41) and the sensor (14).

5. The device (1) according to claim 1, wherein the installation element (8) is formed by at least one rectangular plate.

6. The device (1) according to claim 1, wherein the installation element (8) is a pipe element.

7. The device (1) according to claim 1, wherein the pipe element (8) has no direct contact with an outer wall (3) of the pipe section (2) and is fixed inside the pipe section (2) via the connector (41) and/or a mount of the sensor (14).

8. The device (1) according to claim 1, wherein the sensor (14) is fixed to an outer wall (3) of the pipe section (2) or to the installation element (8).

9. A fuel cell system (100) comprising at least one fuel cell stack (101), an air path (10), wherein air from environment reaches the fuel cell via the air path (10), an exhaust gas line (12), a fuel line (20), wherein fuel is transported to the fuel cell stack (101) via the fuel line (20), and a circulation line (50), wherein the circulation line (50) comprises a purge line (40), wherein a device (1) according to claim 1, is disposed in the exhaust gas line (12).

10. The fuel cell system (100) according to claim 9, wherein the purge line (40) is connected to a connector (41) of the device (1).

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0019] The device according to the invention and the fuel cell system according to the invention are explained in more detail in the following with reference to drawings. Schematically, the figures show:

[0020] FIG. 1 is a schematic topology of a fuel cell system according to a first embodiment example of the invention,

[0021] FIG. 2 illustrates a device for determining the H2 concentration of a fluid in an exhaust gas line of a fuel cell system in a schematic illustration,

[0022] FIG. 3 is a schematic topology of a fuel cell system according to a second embodiment example of the invention and

[0023] FIGS. 4a-4c illustrate devices for determining the H2 concentration of a fluid in an exhaust gas line of a fuel cell system with different installation elements in a schematic illustration and

[0024] FIGS. 5a-5b illustrate a device for determining the H2 concentration of a fluid in an exhaust gas line of a fuel cell system with an installation element configured as a pipe in a schematic illustration.

DETAILED DESCRIPTION

[0025] FIG. 1 shows a schematic topology of a fuel cell system 100 according to a first embodiment example with at least one fuel cell stack 101. The at least one fuel cell stack 101 comprises an air path 10, an exhaust gas line 12 and a fuel line 20. The at least one fuel cell stack 101 can be used for mobile applications with high a power requirement, for example in trucks, or for stationary applications, for example in generators.

[0026] The air path 10 serves as an air supply line for supplying air from the environment to the fuel cell stack 101 via an inlet 16. Components needed for the operation of the fuel cell stack 101 are disposed in the air path 10. An air compressor 11 and/or compressor 11, which compresses and/or draws in the air in accordance with the respective operating conditions of the fuel cell stack 101, is disposed in the air path 10. A humidifier 15 which enriches the air in the air path 10 with a higher concentration of liquid can be disposed downstream of the air compressor 11 and/or compressor 11.

[0027] Further components, such as a filter and/or a heat exchanger and/or valves, can be provided in the air path 10 as well. Air containing oxygen is made available to the fuel cell stack 101 via the air path 10.

[0028] The fuel cell system 100 also comprises an exhaust gas line 12 in which water and other components of the air from the air path 10 are transported into the environment via an outlet 18 after passing through the fuel cell stack 101. The exhaust gas of exhaust gas line 12 can also contain hydrogen (H2), because portions of the hydrogen can diffuse through the membrane of the fuel cell stack 101.

[0029] The fuel cell system 100 can moreover comprise a cooling circuit configured to cool the fuel cell stack 101. The cooling circuit is not shown in FIG. 1 because it is not part of the invention.

[0030] A high pressure tank 21 and a shut-off valve 22 are disposed in the inlet of fuel line 20. Additional components can be disposed in the fuel line 20 to supply fuel to the fuel cell stack 101 as needed.

[0031] To always adequately supply the fuel cell stack 101 with fuel, there is a need for an overstoichiometric metering of fuel via the fuel line 20. The excess fuel, and also certain amounts of water and nitrogen that diffuse through the cell membranes to the anode side, are recirculated in a recirculation line 50 and mixed with the metered fuel from the fuel line 20.

[0032] Various components, such as a jet pump 51 operated with the metered fuel or a blower 52, can be installed to drive the recirculation circuit 50. A combination of jet pump 51 and blower 52 are possible as well.

[0033] Since the amount of water and nitrogen increases more and more over time, the recirculation circuit 50 has to be flushed periodically so that the performance of the fuel cell stack 101 does not decrease due to an excessive concentration of nitrogen in the fuel line 20.

[0034] A purge line 40 is disposed between the circulation line 50 and the exhaust gas line 12 so that the gas mixture can flow from the circulation line 50 into the exhaust gas line 12.

[0035] A purge valve 44 which can open and close the connection between the circulation line 50 and the exhaust gas line 12 can be disposed in the purge line 40. The purge valve 44 is typically opened for a short period of time, so that the gas mixture is fed into the exhaust gas line 12 via the purge line 40.

[0036] According to one embodiment of the invention, a device 1 for determining the H2 concentration is disposed in the exhaust gas line 12.

[0037] FIG. 2 shows a device 1 for determining the H2 concentration in a schematic illustration. The device 1 is formed by a pipe section 2 comprising a sensor 14, which can measure the hydrogen concentration in a fluid. The pipe section 2 comprises an inflow opening 4 and an outflow opening 6. Also disposed in the pipe section 2 is an installation element 8 which divides the exhaust gas that has passed through the inflow opening 4 into a first volumetric flow that flows through a first pipe volume V1 and a second volumetric flow that flows through a second pipe volume V2.

[0038] In a further embodiment of the invention, the pipe section 2 can comprise a connector 41 for the purge line 40. The connector 41 establishes a connection between the first volume V1 and the purge line 40. The purge gas of the purge line 40 is directed through the connector 41 into the first volume V1.

[0039] The connector 41 for the purge line 40 is disposed between the inflow opening 4 and the sensor 14, so that, when measuring, the sensor 14 measures the H2 concentration from both the exhaust gas line 12 and the purge line 40.

[0040] FIG. 1 shows a fuel cell system 100 comprising a device without a connector 41, in which the purge line 40 opens into the exhaust gas line 12 in front of the device 1 in the direction of flow.

[0041] FIG. 3 shows a fuel cell system 100 comprising a device 1 with a connector 41. Here the purge line 40 is connected to the connector 41, so that the purge gas can flow directly from the purge line 40 via the connector 41 into the first volume V1 of the pipe section 2.

[0042] In order to achieve the best possible mixing of the exhaust gas from the exhaust gas line 12 and the purge gas from the purge line 40, a swirl element can be disposed in the first pipe volume V1 between the connector 41 and the sensor 14.

[0043] FIG. 4 shows a cross-section through three devices 1 comprising different installation elements 4, which are each formed by at least one rectangular plate.

[0044] In FIG. 4 a), a rectangular sheet is disposed parallel to a perpendicular bisector (indicated by the dashed line) of the pipe section 2, so that a smaller first pipe volume V1 and a larger second pipe volume V2 are formed.

[0045] In FIG. 4 b), three rectangular plates are disposed parallel to a perpendicular bisector (indicated by the dashed line) of the pipe section 2, so that four pipe volumes V1, V2, V3 and V4 are formed.

[0046] In FIG. 4 c), three rectangular plates are disposed parallel to a perpendicular bisector (indicated by the dashed line) of the pipe section 2 and two rectangular plates have additionally been disposed perpendicular to the perpendicular bisector, so that twelve pipe volumes V1, V2, V3, . . . , V12 are formed.

[0047] FIG. 5 shows an embodiment of the device 1 in which the installation element 8 is formed by a pipe element. FIG. 5 a) shows a cross-section through the device 1, in which the sectional plane has been selected perpendicular to the main flow direction. FIG. 5 b) shows a cross-section through the device 1, in which the sectional plane has been selected parallel to the main flow direction.

[0048] In the shown embodiment example, the installation element 8 is a circular pipe element, which is disposed in the pipe volume in such a way that two concentric circles are formed in the sectional plane. The first pipe volume V1 can be selected inside the pipe element 8, as shown.

[0049] The pipe element 8 has no direct contact with the outer wall 3 of the pipe section 2 and is fixed inside the pipe section 2 via the connector 41 and/or a mount of the sensor 14.

[0050] The sensor 14 can be attached to an outer wall 3 of the pipe section 2 or to the installation element 8, depending on the selection of the first pipe volume V1. The sensor can also be attached to the outer wall 3, so that measurements are carried out in the volume V2.