Method for operating a tank system

Abstract

The invention relates to a method for operating a tank system (10) comprising a number of at least two tanks (21, 22, 23, 24, 25), which are connected in parallel and which contain a gaseous substance, and in which an interior pressure (PX) prevails, for supplying a consumer unit (12), which requires a full load volume of the gaseous substance, wherein each tank (21, 22, 23, 24, 25) has a safety valve (31, 32, 33, 34, 35), which shuts down the tank if a flow volume of the gaseous material through the safety valve (31, 32, 33, 34, 35) exceeds a shut-off volume. If the interior pressure (PX) in at least one tank (21, 22, 23, 24, 25) falls below a first threshold, at least one other tank (21, 22, 23, 24, 25) that was previously shut down is connected.

Claims

1. A method for operating a tank system for supplying a consumer unit, wherein the consumer unit requires no more than a full load amount of a gaseous substance, the method comprising providing the tank system comprising a plurality of tanks which are fluidly connectable, in parallel, to the consumer unit, wherein the tanks contain the gaseous substance at an internal pressure, providing each tank of the plurality of tanks with a respective safety valve that fluidly disconnects the tank from the consumer unit if a throughflow amount of the gaseous substance through the safety valve exceeds a shut-off amount, fluidly connecting to the consumer unit, when the internal pressure in at least one tank fluidly connected to the consumer unit is less than a first threshold value another tank that was not previously connected to the consumer unit, and fluidly disconnecting from the consumer unit, when the internal pressure in at least one of the tanks fluidly connected to the consumer unit exceeds the first threshold value, at least one tank other than the tank having the internal pressure that exceeds the first threshold value, wherein the fluidly connecting and the fluidly disconnecting result in a higher average internal pressure of the tanks connected to the consumer unit such that a leak of the gaseous substance through the safety valves is more easily detectable.

2. The method as claimed in claim 1, wherein the safety valves are configured to shut off at a specified minimum pressure, which is lower than the first threshold value, and which is calculated such that a sum of the shut-off amounts of the safety valves of all the tanks for a minimum pressure is greater than the full load amount.

3. The method as claimed in claim 2, wherein when the internal pressure in all the plurality of tanks exceeds the minimum pressured at least as many tanks are fluidly connected to the consumer unit such that the sum of the shut-off amounts of the safety valves of the tanks that are fluidly connected to the consumer unit is greater than the full load amount.

4. The method as claimed in claim 1, wherein the first threshold value is calculated such that the shut-off amount of the safety valve at the first threshold value is greater than the full load amount.

5. The method as claimed in claim 4, wherein when the internal pressure in at least one tank connected to the consumer unit exceeds the first threshold value, exactly one tank, the internal pressure of which exceeds the first threshold value, is fluidly connected to the consumer unit.

6. The method as claimed in claim 1, wherein the exactly one tank is fluidly disconnected from the consumer unit when the internal pressure of the exactly one tank is less than the first threshold value.

7. The method as claimed in claim 1, wherein when the internal pressure in all the plurality of tanks is less than the first threshold value and exceeds a second threshold value in at least two of the plurality tanks, exactly two of the plurality of tanks, the internal pressures of which are less than the first threshold value and exceed the second threshold value, are fluidly connected to the consumer unit.

8. The method as claimed in claim 7, wherein the second threshold value is calculated such that the shut-off amount of the safety valves at the second threshold value is greater than half the full load amount.

9. The method as claimed in claim 7, wherein the exactly two tanks are fluidly disconnected from the consumer unit if the internal pressure of both of the exactly two tanks is less than the second threshold value.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

(1) Embodiments of the invention are described in detail using the drawings and the subsequent description.

(2) In the figures:

(3) FIG. 1 shows a schematic representation of a tank system connected to a consumer unit,

(4) FIG. 2 shows a graphical representation of the dependency of the shut-off amount of a safety valve on an internal pressure in a tank,

(5) FIG. 3 shows a flow chart of a first operating strategy for the tank system,

(6) FIG. 4 shows a flow chart of a second operating strategy for the tank system and

(7) FIG. 5 shows a graphical representation of the dependency of the number of tanks that are connected on the internal pressure in the tanks.

DETAILED DESCRIPTION

(8) In the following description of the embodiments of the invention, identical or similar elements are denoted by the same reference characters, wherein a repeated description of said elements in individual cases is omitted. The figures represent the subject matter of the invention only schematically.

(9) FIG. 1 shows a schematic representation of a tank system 10 that is connected to a consumer unit 12. The tank system 10 comprises in the present case a first tank 21, a second tank 22, a third tank 23, a fourth tank 24 and a fifth tank 25. In general, the tank system 10 comprises a number N of tanks 21, 22, 23, 24, 25. N be any whole number greater than or equal to two, in the present case N equals five.

(10) The first tank 21 comprises a first control valve 41 and a first safety valve 31. The second tank 22 comprises a second control valve 42 and a second safety valve 32. The third tank 23 comprises a third control valve 43 and a third safety valve 33. The fourth tank 24 comprises a fourth control valve 44 and a fourth safety valve 34. The fifth tank 25 comprises a fifth control valve 45 and a fifth safety valve 35.

(11) The tanks 21, 22, 23, 24, 25 contain a gaseous substance, in the present case hydrogen (H.sub.2), which is under pressure. An internal pressure PX thus prevails in each of the tanks 21, 22, 23, 24, 25. The tanks 21, 22, 23, 24, 25 are connected in parallel and are connected to a collecting line 14. The collecting line 14 is also connected to the consumer unit 12, which in the present case is a fuel cell system. By means of the collecting line 14, the consumer unit 12 can be supplied with the gaseous substance from the tanks 21, 22, 23, 24, 25 of the tank system 10.

(12) By means of the control valves 41, 42, 43, 44, 45, which in the present case are embodied as solenoid valves, the tanks 21, 22, 23, 24, 25 can be connected and disconnected mutually independently. In this case, a tank 21, 22, 23, 24, 25 is connected if it is connected to the collecting line 14 and thus also to the consumer unit 12. A tank 21, 22, 23, 24, 25 is disconnected if it is not connected to the collecting line 14 and the consumer unit 12.

(13) The safety valves 31, 32, 33, 34, 35 disconnect the respective tank 21, 22, 23, 24, 25 if a throughflow amount of the gaseous substance through the safety valve 31, 32, 33, 34, 35 exceeds a shut-off amount MA. The safety valves 31, 32, 33, 34, 35 disconnect the respective tank 21, 22, 23, 24, 25 in particular if the throughflow amount is greater than the shut-off amount MA because of a leak, for example in the collecting line 14. The shut-off amount MA of the safety valves 31, 32, 33, 34, 35 is not constant but is a function of the internal pressure PX of the tanks 21, 22, 23, 24, 25.

(14) FIG. 2 shows a graphical representation of the dependency of the shut-off amount MA of a safety valve 31, 32, 33, 34, 35 on an internal pressure PX in a tank 21, 22, 23, 24, 25. In this case, the internal pressure PX is plotted on the X-axis and the shut-off amount MA is plotted on the Y-axis. In the present case, the tanks 21, 22, 23, 24, 25 of the tank system 10 are of the same design and the safety valves 31, 32, 33, 34, 35 are also of the same design. The shut-off amounts MA of the safety valves 31, 32, 33, 34, 35 are also equal.

(15) The consumer unit 12 requires no more than a full load amount MV of the gaseous substance. The safety valves 31, 32, 33, 34, 35 are adjusted so that the sum of the shut-off amounts MA of all the safety valves 31, 32, 33, 34, 35 for a minimum pressure PM corresponds to a maximum amount MM, which is greater than the full load amount MV.

(16) The minimum pressure PM at which emptying the tanks 21, 22, 23, 24, 25 for supplying the consumer unit 12 is still possible amounts to 15 bar in the present case. In the present case, the full load amount MV is approximately 4 g/s. The shut-off amount MA of the safety valves 31, 32, 33, 34, 35 for the minimum pressure PM is approximately 1 g/s in the present case. The maximum amount MM is thus approximately 5 g/s in the present case.

(17) In general, the following applies:
MM=N*MA(PM)>MV

(18) At a first threshold value P1, in the present case approximately 375 bar, the shut-off amount MA of the safety valves 31, 32, 33, 34, 35 equals the maximum amount MM. At a second threshold value P2, in the present case approximately 94 bar, the shut-off amount MA of the safety valves 31, 32, 33, 34, 35 is half the maximum amount MM. At a third threshold value P3, in the present case approximately 42 bar, the shut-off amount MA of the safety valves 31, 32, 33, 34, 35 is a third of the maximum amount MM. At a fourth threshold value P4, in the present case approximately 23 bar, the shut-off amount MA of the safety valves 31, 32, 33, 34, 35 is a quarter of the maximum amount MM.

(19) FIG. 3 shows a flow chart of a first operating strategy for the tank system 10. Initially a first condition 101 is checked, according to which the internal pressure PX in at least one tank 21, 22, 23, 24, 25 exceeds the first threshold value P1.

(20) If the first condition 101 is met, then in a first implementation step 103 exactly one of the tanks 21, 22, 23, 24, 25 is connected, the internal pressure PX of which exceeds the first threshold value P1. At the same time, the remaining tanks 21, 22, 23, 24, 25 are disconnected. After the first implementation step 103, exactly one tank 21, 22, 23, 24, 25 of the tank system 10 is thus connected.

(21) Subsequently, in a first test step 105 the internal pressure PX is measured of the tanks 21, 22, 23, 24, 25 of the tank system 10 that are connected. If the internal pressure PX of the tank that is connected 21, 22, 23, 24, 25 still exceeds the first threshold value P1, said tank 21, 22, 23, 24, 25 remains connected.

(22) If the internal pressure PX of the tank that is connected 21, 22, 23, 24, 25 is less than the first threshold value P1, then said tank that is connected 21, 22, 23, 24, 25 is disconnected in a first switching step 107.

(23) Then the first condition 101 is checked again, according to which the internal pressure PX in at least one tank 21, 22, 23, 24, 25 exceeds the first threshold value P1. If the first condition 101 is still met, exactly one other tank 21, 22, 23, 24, 25, the internal pressure PX of which exceeds the first threshold value P1, is connected in the first implementation step 103.

(24) During implementation of the first operating strategy for the tank system 10, exactly one of the tanks 21, 22, 23, 24, 25 of the tank system 10 is thus always connected. As a result, the tanks 21, 22, 23, 24, 25 are emptied successively but approximately uniformly. The internal pressure PX in the individual tanks 21, 22, 23, 24, 25 thus remains approximately equal while the first operating strategy is carried out.

(25) If the first condition 101 is no longer met, i.e. if the internal pressure PX in each tank 21, 22, 23, 24, 25 is less than the first threshold value P1, then the operating strategy for the tank system 10 is changed in a first change step 109.

(26) FIG. 4 shows a flow chart of a second operating strategy for the tank system 10. In preparation, a second condition 201 is checked, according to which the internal pressure PX in all the tanks 21, 22, 23, 24, 25 is less than the first threshold value P1 and exceeds the second threshold value P2 in at least two tanks 21, 22, 23, 24, 25.

(27) If the second condition 201 is met, then in a second implementation step 203 exactly two of the tanks 21, 22, 23, 24, 25, the internal pressure PX of which exceeds the second threshold value P2, are connected. At the same time, the remaining tanks 21, 22, 23, 24, 25 are disconnected. Following the second implementation step 203, exactly two tanks 21, 22, 23, 24, 25 of the tank system 10 are thus connected.

(28) Subsequently, in a second test step 205 the internal pressure PX is measured of the tanks 21, 22, 23, 24, 25 of the tank system 10 that are connected. If the internal pressure PX of the tanks that are connected 21, 22, 23, 24, 25 still exceeds the second threshold value P2, said tanks 21, 22, 23, 24, 25 remain connected.

(29) If the internal pressure PX of the tanks that are connected 21, 22, 23, 24, 25 is less than the second threshold value P2, then said tanks that are connected 21, 22, 23, 24, 25 are disconnected in a second switching step 207.

(30) Then the second condition 201 is checked again, according to which the internal pressure PX in all the tanks 21, 22, 23, 24, 25 is less than the first threshold value P1 and exceeds the second threshold value P2 in at least two tanks 21, 22, 23, 24, 25. If the second condition 201 is still met, exactly two other tanks 21, 22, 23, 24, 25, the internal pressure PX of which exceeds the second threshold value P2, are connected in the second implementation step 203.

(31) During the implementation of the second operating strategy for the tank system 10, exactly two of the tanks 21, 22, 23, 24, 25 of the tank system 10 are thus always connected. As a result, the tanks 21, 22, 23, 24, 25 are emptied successively but approximately uniformly. The internal pressure PX in the individual tanks 21, 22, 23, 24, 25 thus remains approximately equal while the second operating strategy is carried out.

(32) If the second condition 201 is no longer met, i.e. if the internal pressure PX in each tank 21, 22, 23, 24, 25 is less than the second threshold value P2, then the operating strategy for the tank system 10 is changed in a second change step 209.

(33) Similarly to the first and second operating strategies presented here, three, four or five tanks 21, 22, 23, 24, 25 are connected at the same time in further operating strategies that are not explicitly described here. A number i of the tanks that are connected is a function of the internal pressure PX in the tanks 21, 22, 23, 24, 25 in this case.

(34) FIG. 5 shows a graphical representation of the dependency of the number i of the tanks that are connected 21, 22, 23, 24, 25 on the internal pressure PX in the tanks 21, 22, 23, 24, 25. In this case, the internal pressure PX is plotted on the X-axis and the number i of the tanks that are connected 21, 22, 23, 24, 25 is plotted on the Y-axis.

(35) If the internal pressure PX in the tanks 21, 22, 23, 24, 25 exceeds the first threshold value P1, then at least one tank 21, 22, 23, 24, 25, preferably exactly one tank 21, 22, 23, 24, 25, is connected.

(36) If the internal pressure PX in the tanks 21, 22, 23, 24, 25 is less than the first threshold value P1 and exceeds the second threshold value P2, then at least two tanks 21, 22, 23, 24, 25, preferably exactly two tanks 21, 22, 23, 24, 25, are connected.

(37) If the internal pressure PX in the tanks 21, 22, 23, 24, 25 is less than the second threshold value P2 and exceeds the third threshold value P3, then at least three tanks 21, 22, 23, 24, 25, preferably exactly three tanks 21, 22, 23, 24, 25, are connected.

(38) If the internal pressure PX in the tanks 21, 22, 23, 24, 25 is less than the third threshold value P3 and exceeds the fourth threshold value P4, then at least four tanks 21, 22, 23, 24, 25, preferably exactly four tanks 21, 22, 23, 24, 25, are connected.

(39) If the internal pressure PX in the tanks 21, 22, 23, 24, 25 is less than the fourth threshold value P4 and exceeds the minimum pressure PM, then all five tanks 21, 22, 23, 24, 25 are connected.

(40) The invention is not limited to the exemplary embodiments that are described here and the aspects that are emphasized therein. Rather, within the scope specified by the claims, a number of amendments that lie within the scope of expert actions are possible.