# US 10,122,033 B2 · Ascertaining fuel cell inlet humidity by means of pressure sensors, and a mass flow rate-dependent control of the humidifier bypass

> Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt

- Number: US 10,122,033 B2
- Document ID: US10122033B2
- Status: Granted
- Kind: B2
- Application number: 14/435,336
- Filed: 2013-10-07
- Published: 2015-10-15
- Granted: 2018-11-06
- Earliest claimed: 2012-10-12
- Assignees: Robert Bosch GmbH
- Applicants: Robert Bosch GmbH
- Inventors: David Knies; Daniel Zirkel
- Web page: https://patentgrep.com/patent/US10122033B2

## CPC

- H01M 8/04492: Humidity; Ambient humidity; Water content
- H01M 8/04126: {Humidifying}
- H01M 8/04141: {by water containing exhaust gases}
- H01M 8/04149: {by diffusion, e.g. making use of membranes}
- H01M 8/0438: Pressure; Ambient pressure; Flow
- H01M 8/04544: {Voltage}
- H01M 8/04746: Pressure; Flow
- H01M 8/04835: {of fuel cell reactants}
- Y02E 60/50: Fuel cells
- H01M: PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION

## Abstract

The invention relates to a fuel cell arrangement (1) having at least one fuel cell (2) with a cathode (3) and an anode. The cathode (3) and the anode each have a reactant feed (4) and a reactant discharge (5), a humidifying device (10) and sensors (12, 13, 14) being provided at least at one of the reactant feeds (4). In particular, the sensors (12, 13, 14) are at least one fluid mass sensor (12) and two pressure sensors (13, 14), the fluid mass sensor (12) and one of the pressure sensors (13) being arranged upstream of the humidifying device (10) and one of the pressure sensors (14) being arranged downstream of the humidifying device (10). The humidifying device (10) can be operated in a controlled manner on the basis of the measurements of the sensors (12, 13, 14). The invention further relates to a method for controlling the humidity of a reactant for such a fuel cell arrangement (1).

## Claims

### Claim 1

A fuel cell arrangement (1) comprising at least one fuel cell (2) with a cathode (3) and an anode, wherein the cathode (3) and the anode each have a reactant feed (4) and a reactant discharge (5), a humidifying device (10) and sensors (12, 13, 14) being provided at least at one of the reactant feeds (4), characterized in that the sensors (12, 13, 14) are at least one fluid mass sensor (12) and two pressure sensors (13, 14), the fluid mass sensor (12) and one of the pressure sensors (13) being arranged upstream of the humidifying device (10) and one of the pressure sensors (14) being arranged downstream of the humidifying device (10), and in that the humidifying device (10) is configured to be operated in a controlled manner on the basis of the measurements of the sensors (12, 13, 14), and wherein a bypass line (16) is provided in the at least one reactant feed (4), which bypass line is configured to be controlled by means of a valve (15) and by means of which bypass line the humidifying device (10) is configured to be at least partially bypassed, and further wherein the bypass line is connected to the reactant feed at a point downstream of the humidifying device and upstream of the one of the pressure sensors being arranged downstream of the humidifying device, wherein a control circuit programmed to calculate humidity as linearly dependent on a measured fluid mass flow rate and linearly dependent on a difference between measured pressures is configured to determine the humidity of the reactant in the at least one of the reactant feeds on the basis of measurement values from no sensors other than the fluid mass sensor and the two pressure sensors.

### Claim 2 (depends on 1)

The fuel cell arrangement (1) according to claim 1, characterized in that the sensors (12, 13, 14) and the humidifying device (10) are arranged in the reactant feed (4) of the cathode (3).

### Claim 3 (depends on 1)

The fuel cell arrangement (1) according to claim 1, characterized in that the humidifying device (10) is a gas-gas humidifier.

### Claim 4 (depends on 3)

The fuel cell arrangement (1) according to claim 3, characterized in that the gas-gas humidifier is also connected to a corresponding reactant discharge (5) of the fuel cell (2).

### Claim 5 (depends on 1)

A method for controlling the humidity at a reactant for a fuel cell arrangement (1), the fuel cell arrangement (1) being configured according to claim 1, the method comprising calculating the humidity of the reactant in the at least one reactant feed (4) on the basis of measurement values of the sensors (12, 13, l4), characterized in that the calculated humidity is calculated linearly dependent on a measured fluid mass flow rate and linearly dependent on a difference between measured pressures.

### Claim 6 (depends on 5)

The method for controlling the humidity of a reactant for a fuel cell arrangement (1) according to claim 5, characterized in that a bypass line (16) is provided in the at least one reactant feed (4), wherein the humidifying device (10) is at least partially bypassed by means of the bypass line (16) and said bypass line is controlled by means of a valve (15), the valve (15) being controlled on the basis of the measured fluid mass flow rate and the measured pressures.

### Claim 7 (depends on 6)

The method for controlling the humidity of a reactant for a fuel cell arrangement (1) according to claim 6, characterized in that the valve (15) is controlled by means of a control voltage and in that the control voltage is calculated only from the measured fluid mass flow rate.

### Claim 8 (depends on 7)

The method for controlling the humidity of a reactant for a fuel cell arrangement (1) according to claim 7, characterized in that the control voltage is calculated linearly dependent on the measured fluid mass flow rate.

### Claim 9 (depends on 5)

The method for controlling the humidity of a reactant for a fuel cell arrangement (1) according to claim 5, wherein the humidity of the reactant in the at least one reactant feed (4) is approximately calculated on the basis of the measurement values of the sensors (12, 13, 14).
