Device for the Combined Reduction of the Carbon Dioxide and Water or Moisture Content, Motor Vehicle, and Method
20220016567 · 2022-01-20
Inventors
- Gelase MBADINGA MOUANDA (Sachsenheim, DE)
- Thomas JESSBERGER (Asperg, DE)
- Achim Janner (Ludwigsburg, DE)
Cpc classification
B60H2003/0691
PERFORMING OPERATIONS; TRANSPORTING
B01D2259/4566
PERFORMING OPERATIONS; TRANSPORTING
B01D53/0446
PERFORMING OPERATIONS; TRANSPORTING
B60H2003/028
PERFORMING OPERATIONS; TRANSPORTING
F24F13/28
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B01D53/0462
PERFORMING OPERATIONS; TRANSPORTING
Y02C20/40
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
B60H3/0633
PERFORMING OPERATIONS; TRANSPORTING
B01D2257/404
PERFORMING OPERATIONS; TRANSPORTING
A61L2209/22
HUMAN NECESSITIES
B60H3/024
PERFORMING OPERATIONS; TRANSPORTING
B01D2257/708
PERFORMING OPERATIONS; TRANSPORTING
B01D2259/40096
PERFORMING OPERATIONS; TRANSPORTING
International classification
Abstract
A device for reducing a carbon dioxide and water content in an enclosed air volume has first and second sorption units for sorbing carbon dioxide and water. The first and second sorption units can be transferred from a sorption mode into a desorption mode and vice versa. In the sorption mode, the first and second sorption units sorb carbon dioxide and water from raw air of the enclosed air volume. In the desorption mode, the first and second desorption units desorb carbon dioxide and water to supplied regeneration air. An air distribution device can switch the first and second sorption units, based on the carbon dioxide and water content, alternately from sorption mode into desorption mode such that, in at least one operating state of the device, one of the first and second sorption units is in sorption mode while the other is in desorption mode.
Claims
1. A device for combined reduction of a carbon dioxide and water content in an enclosed air volume, the device comprising: a first sorption unit configured to sorb carbon dioxide and water; a second sorption unit configured to sorb carbon dioxide and water; wherein the first sorption unit and the second sorption unit each comprise a plurality of sorbents; wherein the first sorption unit and the second sorption unit each are configured to be transferred from a sorption mode into a desorption mode and from the desorption mode into the sorption mode, wherein, in the sorption mode, the first sorption unit and the second sorption unit each sorb carbon dioxide and water from a raw air of the enclosed air volume, and wherein, in the desorption mode, the first sorption unit and the second desorption unit each desorb carbon dioxide and water to a supplied regeneration air; an air distribution device configured to switch the first sorption unit and the second sorption unit, as a function of the carbon dioxide and water content in the enclosed air volume, alternately from the sorption mode into the desorption mode and from the desorption mode into the sorption mode such that, in at least one operating state of the device, one of the first and second sorption units is in the sorption mode while the other one of the first and second sorption units is in the desorption mode.
2. The device according to claim 1, wherein, in the desorption mode, the supplied regeneration air guided through the first or second sorption unit which is in the desorption mode is supplied as loaded regeneration air into an environment of the enclosed air volume.
3. The device according to claim 1, wherein the air distribution device comprises a plurality of valves configured to be switched such that, in operation of the device, the first or second sorption unit which is in the sorption mode is supplied with the raw air from the enclosed air volume to remove the carbon dioxide and the water from the raw air, and wherein the first or second sorption unit which is in the desorption mode is supplied with the supplied regeneration air to remove the carbon dioxide and the water from the first or second sorption unit which is in the desorption mode.
4. The device according to claim 1, further comprising one or more heating elements associated with the first and second sorption units and configured to introduce heat into the first or second sorption unit which is in the desorption mode.
5. The device according to claim 4, wherein the first sorption unit and the second sorption unit each have integrated therein one of the heating elements.
6. The device according to claim 4, wherein the one or more heating elements are positioned upstream of the first and second sorption units.
7. The device according to claim 1, wherein the first sorption unit and the second sorption unit comprise a common heating element configured to introduce heat into the first or second sorption unit which is in the desorption mode.
8. The device according to claim 1, further comprising a regeneration valve comprising a first switch position, a second switch position, and a third switch position, wherein, in the first switch position, the first or second sorption unit which is in the desorption mode is supplied with the supplied regeneration air removed from an environment of the enclosed air volume, wherein, in the second switch position, the first or second sorption unit which is in the desorption mode is supplied with supplied regeneration air removed from the enclosed air volume, and wherein, in the third switch position, the first or second sorption unit which is in the desorption mode is regenerated under vacuum.
9. The device according to claim 8, further comprising a desorption blower device configured to supply the supplied regeneration air to the first or second sorption unit which is in the desorption mode, wherein, downstream at a pressure side of the desorption blower device, a desorption conduit is arranged, wherein the desorption conduit comprises a branch that opens into a recirculation conduit, wherein the regeneration valve comprises an inlet and an outlet, wherein a regeneration air conduit is connected to the outlet of the regeneration valve, wherein the recirculation conduit is connected in fluid communication to the inlet of the regeneration valve or the recirculation conduit is connected in fluid communication to the regeneration air conduit downstream of the outlet of the regeneration valve.
10. The device according to claim 9, further comprising a recirculation valve configured to switch the branch so that the supplied regeneration air is selectively recirculated through the first and second sorption units or the supplied regeneration air is guided into the environment of the enclosed air volume via the desorption conduit.
11. The device according to claim 9, wherein the recirculation conduit is connected in fluid communication to the regeneration valve, wherein the regeneration valve comprises a fourth switch position, wherein, in the fourth switch position, the first or second sorption unit which is in the desorption mode is supplied with the supplied regeneration air from the recirculation conduit.
12. The device according to claim 9, further comprising a throttle valve arranged in fluid communication between the outlet of the regeneration valve and a location where the recirculation conduit is connected to the regeneration air conduit.
13. The device according to claim 1, further comprising a blower device configured to supply the raw air to the first or second sorption unit which is in the sorption mode.
14. The device according to claim 13, wherein the blower device is part of an air conditioning device.
15. The device according to claim 1, further comprising a desorption blower device configured to supply the supplied regeneration air to the first or second sorption unit which is in the desorption mode, wherein the desorption blower device is arranged at a pressure side or at a suction side in relation to the first and second sorption units.
16. The device according to claim 1, further comprising a first bypass conduit and a first bypass valve configured to be selectively switched from a first switch state of the first bypass valve into a second switch state of the first bypass valve and from the second switch state of the first bypass valve into the first switch state of the first bypass valve , wherein, in the first switch state of the first bypass valve, the raw air is supplied to the first or second sorption unit which is in the sorption mode, and wherein, in the second switch state of the first bypass valve, the raw air is guided via the first bypass conduit around the first and second sorption units back into the enclosed air volume.
17. The device according to claim 16, further comprising a second bypass conduit and a second bypass valve configured to be selectively switched from a first switch state of the second bypass valve into a second switch state of the second bypass valve and from the second switch state of the second bypass valve into the first switch state of the second bypass valve, wherein, in the first switch state of the second bypass valve, the supplied regeneration air is supplied to the first or second sorption unit which is in the desorption mode, and wherein, in the second switch state of the second bypass valve, the supplied regeneration air is supplied via the second bypass conduit by bypassing the first and second sorption units into the environment of the enclosed air volume.
18. The device according to claim 1, further comprising a bypass conduit and a bypass valve configured to be selectively switched from a first switch state into a second switch state and from the second switch state into the first switch state, wherein, in the first switch state, the supplied regeneration air is supplied to the first or second sorption unit which is in the desorption mode, and wherein, in the second switch state, the supplied regeneration air is supplied via the bypass conduit by bypassing the first and second sorption units into the environment of the enclosed air volume.
19. The device according to claim 1, wherein the first sorption unit and the second sorption unit are configured to remove fine particles, nitrogen oxides and/or volatile organic compounds from the raw air.
20. The device according to claim 19, wherein the plurality of sorbents include a first sorbent configured to adsorb carbon dioxide, a second sorbent configured to adsorb water, and third sorbents configured to remove fine particles, nitrogen oxides and/or volatile organic compounds from the raw air.
21. The device according to claim 20, wherein the third sorbents are arranged between two carrier layers, or the first, second, and third sorbents are mixed with each other.
22. The device according to claim 1, wherein the first and second sorption units are configured to remove allergens, bacteria and/or viruses from the raw air.
23. A motor vehicle comprising a device according to claim 1, wherein the device is configured to be controlled, based on an occupation state of the enclosed air volume with passengers, to maintain the carbon dioxide and water content in the enclosed air volume in a predetermined tolerance field independent of the occupation state.
24. A method for operating a device for combined reduction of a carbon dioxide and water content in an enclosed air volume, wherein the device comprises a first sorption unit configured to sorb carbon dioxide and water, a second sorption unit configured to sorb carbon dioxide and water, and an air distribution device configured to alternately switch the first and second sorption units from a sorption mode into a desorption mode and from the desorption mode into the sorption mode, the method comprising the steps: a) switching one of the first and second sorption units, as a function of the carbon dioxide and water content in the enclosed air volume, by the air distribution device into the sorption mode to sorb carbon dioxide and water from a raw air of the enclosed air volume; b) switching the other one of the first and second sorption units by the air distribution device into the desorption mode to desorb carbon dioxide and water into a supplied regeneration air; and c) alternately performing the steps a) and b) such that, in at least one operating state, one of the first and second sorption units is operated in the sorption mode while the other one of the first and second sorption units is operated in the desorption mode.
25. The method according to claim 24, further comprising introducing heat into the first or second sorption unit operated in the desorption mode.
26. The method according to claim 24, further comprising measuring in the enclosed air volume the carbon dioxide and water content and controlling, based on the measured carbon dioxide and water content, the device such that the carbon dioxide and water content in the enclosed air volume is maintained within a predetermined tolerance field.
27. The method according to claim 26, further comprising detecting an occupation state of the enclosed air volume with passengers and controlling, based on the detected occupation state of the enclosed air volume with passengers, the device such that the carbon dioxide and water content in the enclosed air volume is maintained in a predetermined tolerance field.
28. The method according to claim 24, further comprising performing the desorption mode by removing the regeneration air from an environment of the enclosed air volume, or by removing the regeneration air from the enclosed air volume, or by applying a vacuum, or by recirculating the regeneration air.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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[0073] In the Figures, same or functionally the same elements, if nothing to the contrary is mentioned, have been provided with same reference characters.
PREFERRED EMBODIMENTS
[0074]
[0075] The enclosed air volume 3 is an interior or passenger compartment of the motor vehicle 1. The enclosed air volume 3 can however also be associated with a watercraft, a construction machine or a construction vehicle, a rail vehicle, an agricultural machine or an agricultural vehicle, or an aircraft. The enclosed air volume 3 can however also be part of a building or of a stationary machine.
[0076] In the following, it is however presumed that the enclosed air volume 3 is the passenger compartment of the motor vehicle 1. Therefore, the enclosed air volume 3 will be referred to in the following as passenger compartment. The passenger compartment 3 can be air-conditioned by means of an air conditioning device 4 (English: heating, ventilation, and air conditioning, HVAC). For extending a range of such an electrically driven motor vehicle 1, an energy savings as large as possible is aimed at. In reference to the air conditioning device 4, this means that the latter, for the purpose of air conditioning the passenger compartment 3, should take in as little fresh air as possible from the environment U of the motor vehicle 1.
[0077] When using recirculated air removed from the passenger compartment 3 for air conditioning the passenger compartment 3, it is however possible that water (H.sub.2O) that is contained in the exhalation air of occupants or passengers can accumulate in the passenger compartment 3 which leads to fogging of window panes, for example, of a windshield or of side windows, of the motor vehicle 1. This is to be prevented or at least to be reduced with respect to safety aspects. Moreover, also carbon dioxide (CO.sub.2) that is contained in the exhalation air can accumulate in the passenger compartment 3. This can lead to loss of concentration or even health impairments of the occupants. This also is to be prevented or at least reduced with respect to safety aspects as well as with respect to health aspects.
[0078]
[0079] The device 5 comprises a first sorption unit 6 as well as a second sorption unit 7. “Sorption” is a collective term for processes that lead to an accumulation of a substance within a phase or at a boundary surface between two phases. The accumulation within a phase is referred to more precisely as absorption, that at a boundary surface as adsorption. This means the sorption units 6, 7 are suitable to adsorb and/or to absorb substances such as CO.sub.2 and H.sub.2O but also nitrogen oxides (NOX) and/or volatile organic compounds (English: volatile organic compounds, VOCs). Examples of volatile organic compounds are higher hydrocarbons. The sorption units 6, 7 can also be suitable to adsorb and/or absorb sulfur dioxide (SO.sub.2). Preferably, the sorption units 6, 7 are however pure adsorption units or can be referred to as such.
[0080] The sorption units 6, 7 are preferably exchangeable, and can be operated, as will be explained in the following, alternately in a sorption mode M1 and in a desorption mode M2. The sorption units 6, 7 are cartridge-shaped and can be referred to as cartridges or sorption cartridges. The sorption mode M1 can also be referred to as adsorption mode. The desorption mode M2 can also be referred to as regeneration mode. This means that the first sorption unit 6 is in the sorption mode M1 when the second sorption unit 7 is in the desorption mode M2 and vice versa. Thus, the two sorption units 6, 7 are never simultaneously in the same mode M1, M2. Preferably, the sorption units 6, 7 each comprise a cartridge form so that they are easily exchangeable.
[0081] Each sorption unit 6, 7 comprises a first sorbent 8 and a second sorbent 9. Preferably, the sorbents 8, 9 are adsorbents or can be referred to as such. For example, the first sorbent 8 is suitable to adsorb CO.sub.2. Accordingly, the second sorbent 9 can be suitable to adsorb H.sub.2O. The two sorbents 8, 9 can thus remove H.sub.2O and CO.sub.2 from the passenger compartment 3. The first sorbent 8 is illustrated with small circles. The second sorbent 9 is illustrated with large circles. It is also possible to provide further sorbents that are suitable, for example, to sorb NOX or VOCs. Thus, an arbitrary number of different sorbents 8, 9 can be provided for processing the recirculated air in the passenger compartment 3.
[0082] For example, in addition to the sorbents 8, 9, at least one further sorbent or also a plurality of further sorbents (not illustrated) are provided that are suitable to remove fine particles, NOx and/or VOCs from the raw air RO. The further sorbents can be introduced between two carrier layers, in particular carrier layers of a nonwoven. Alternatively, the sorbents 8, 9 and the further sorbents can be mixed with each other. The further sorbents can comprise active carbon which, in particular in form of a bulk material, is introduced preferably between the two carrier layers. The further sorbent or the further sorbents can be mixed with the first sorbent 8 and/or with the second sorbent 9 in order to construct one or a plurality of mixed bulk materials.
[0083] Furthermore, the sorption units 6, 7 can also be suitable to remove, aside from CO.sub.2 and H.sub.2O, also allergens, bacteria and/or viruses from the raw air RO. This can be realized by a functional coating of carrier materials, for example, of nonwovens, or by a functional coating of the sorbents 8, 9. Moreover, the sorption units 6, 7 can comprise in regard to a comfort aspect at least one scent component.
[0084] The sorbents 8, 9 can each be in the form of spherical granular material. Preferably, the sorbents 8, 9 are fixed on a carrier material or fixed by means of a carrier material. The sorption units 6, 7 each can have a cylindrical, in particular a hollow cylindrical, a pie-shaped or a rectangular geometry. A “pie-shaped” geometry is to be understood presently in particular as a flat circular cylindrical geometry.
[0085] In
[0086] The first sorption unit 6 has correlated therewith an optional first heating element 11 with which the sorbents 8, 9 can be supplied with heat Q. In the sorption mode M1, the first heating element 11 is inactive so that it does not supply the first sorption unit 6 with heat Q. The first heating element 11 can be a heating wire which extends through the first sorption unit 6 and is supplied with current for introducing the heat Q and to thus heat the sorbents 8, 9. The heat Q can however be introduced also by any other way. For example, the heat Q can also be waste heat of an electric motor for driving the motor vehicle 1. The heat Q can also be waste heat of a conventional internal combustion engine, of a battery cooling system or of a fuel cell cooling circuit. The first heating element 11 can also be a heat exchanger or can comprise a heat exchanger.
[0087] In the desorption mode M2, the second sorption unit 7 is supplied with regeneration air R1 which is not loaded with CO.sub.2 and H.sub.2O. For this purpose, a second blower device 12 can be used. That the non-loaded regeneration air R1 is “non-loaded” with CO.sub.2 and H.sub.2O is to be understood such that the non-loaded regeneration air R1 is capable of taking up CO.sub.2 and H.sub.2O stored in the second sorption unit 7. This means that the non-loaded regeneration air R1 can comprise a certain content of CO.sub.2 and H.sub.2O. However, the non-loaded regeneration air R1 is not saturated with CO.sub.2 and H.sub.2O. The non-loaded regeneration air R1 can be removed, for example, from the passenger compartment 3 or from the environment U.
[0088] Moreover, an optional second heating element 13 is also provided by means of which the second sorption unit 7 in the desorption mode M2 is heated and heat Q is thus introduced into the second sorption unit 7. The first heating element 11 and the second heating element 13 are preferably of identical construction and are operated alternately. As mentioned before, the heat Q can be supplied, for example, also in the form of waste heat of an electric motor. The heat Q, as also mentioned before, can however also be waste heat of a conventional internal combustion engine, of a battery cooling system or of a fuel cell cooling circuit. The second heating element 13 can also be a heat exchanger or can comprise a heat exchanger.
[0089] Upon heating the sorbents 8, 9 in the desorption mode M2 of the second sorption unit 7, they release CO.sub.2 and H.sub.2O into the non-loaded regeneration air R1. This means that CO.sub.2 and H.sub.2O are desorbed. Preferably, a temperature of above 55° C. is required for desorption. The non-loaded regeneration air R1 is guided through the second sorption unit 7, there takes up CO.sub.2 and H.sub.2O, and is then discharged from the second sorption unit 7 as loaded regeneration air R2. In particular, the loaded regeneration air R2 is supplied to the environment U.
[0090]
[0091] In operation of the motor vehicle 1, the interior air IL in the passenger compartment 3 is loaded with CO.sub.2 and H.sub.2O. The loaded interior air IL is the aforementioned raw air RO. This aforementioned raw air RO can be supplied via a conduit 16 at least partially to the environment U. Moreover, the raw air RO loaded with CO.sub.2 and H.sub.2O can be supplied by means of a conduit 17 at least partially to the device 5. In particular, the conduit 17 supplies the raw air RO to the first blower device 10. The first blower device 10 is mounted at the pressure side. The first blower device 10 can however also be mounted at the suction side.
[0092] Downstream of the first blower device 10, a conduit 18 is provided which supplies the raw air RO to an air distribution device 19. The air distribution device 19 comprises a plurality of valves 20 to 23, in particular three-way valves. The valves 20-23 are preferably embodied as flap valves. Accordingly, the air distribution device 19 can also be referred to as a flap device or flap system.
[0093] The conduit 18 is in fluid communication with the valve 20 that, in turn, is in fluid communication via conduits 24, 25 with the two sorption units 6, 7. Depending on the switched position of the valve 20, the raw air RO can be supplied selectively either to the first sorption unit 6 or to the second sorption unit 7. In or at the conduit 18, a sensor 26, in particular a CO.sub.2, H.sub.2O and/or temperature sensor, can be provided. In particular, the conduit 24 connects the valve 20 to the first sorption unit 6. The conduit 25 connects the valve 20 to the second sorption unit 7.
[0094] Downstream of the sorption units 6, 7, a valve 21 of the air distribution device 19 is provided. The valve 21 is connected by means of a conduit 27 to the first sorption unit 6 and by means of a conduit 28 to the second sorption unit 7. A conduit 29 connects the valve 21 to the passenger compartment 3. The conduit 29 can also comprise a sensor 30, in particular a CO.sub.2, H.sub.2O and/or temperature sensor. By means of the sensor 30, it can be detected, for example, when the sorption unit 6, 7 which is in the sorption mode M1 is exhausted. Between the conduits 18, 29 a bypass conduit 31 for bypassing the sorption units 6, 7 is provided. Moreover, between the conduits 18, 29, a sensor 32, in particular pressure sensor, is provided also which can detect a pressure difference between the conduits 18, 29.
[0095] The air distribution device 19 comprises a further valve 22 which by means of a conduit 33 is connected to the first sorption unit 6 and by means of the conduit 34 to the second sorption unit 7. A check valve 35 as well as a regeneration valve 36 are arranged upstream of the valve 22. The regeneration valve 36 is preferably a three-way valve. The ambient air UL is supplied to the regeneration valve 36 as non-loaded regeneration air R1. Moreover, the interior air IL as non-loaded regeneration air R1 can also be supplied to the regeneration valve 36 via a conduit 37.
[0096] Downstream of the sorption units 6, 7, a further valve 23 of the air distribution device 19 is positioned. The valve 23 is connected by means of a conduit 38 to the first sorption unit 6 and by means of a conduit 39 to the second sorption unit 7. A conduit 40 connects the valve 23 to the second blower device 12. The second blower device 12 is positioned in this context at the suction side, i.e., downstream of the sorption units 6, 7. The second blower device 12 can however also be positioned at the pressure side, i.e., upstream of the sorption units 6, 7. The second blower device 12 discharges the loaded regeneration air R2 into the environment U.
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[0098] Downstream of the second blower device 12, a further sensor 43, in particular a CO.sub.2, H.sub.2O and/or temperature sensor, is provided. Moreover, a further sensor 44, in particular a CO.sub.2, H.sub.2O and/or temperature sensor, is also provided in or at the conduit 40. Moreover, a sensor 45 is provided which is suitable to detect a pressure difference between the conduit 40 and the air distribution device 19. Each sorption unit 6, 7 has correlated therewith a sensor 46, 47, in particular a differential pressure sensor. Also, a sensor 48, in particular as CO.sub.2, H.sub.2O and/or temperature sensor, can be provided in the passenger compartment 3. In order to activate and deactivate the bypass conduit 31, a bypass valve 49 is provided. Moreover, the conduit 40 comprises a pressure sensor 50, in particular for determining the absolute pressure.
[0099] In
[0100] At the same time, the valves 20, 21 are switched such that by means of the first blower device 10 raw air RO loaded with CO.sub.2 and H.sub.2O is sucked in from the passenger compartment 3 and guided through the second sorption unit 7. In the second sorption unit 7, the CO.sub.2 in the H.sub.2O are adsorbed and the non-loaded clean air RL is supplied again to the passenger compartment 3. The bypass valve 49 is switched such that the bypass conduit 31 is inactive.
[0101]
[0102]
[0103] The valves 22, 23 are switched such that the non-loaded regeneration air R1 taken in from the environment U is sucked by means of the second blower device 12 through the second sorption unit 7. The second heating element 13 is in operation in this context. The second blower device 12 blows the regeneration air R2 which is enriched with CO2 and H2O into the environment U.
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[0108] Furthermore, the air conditioning device 4 comprises a valve 52, for example, a flap valve, that can be switched such that either ambient air UL from the environment U or interior air IL from the passenger compartment 3 is sucked in. For temperature control, a cooling element 53 and a heating element 54 are provided. Moreover, the air conditioning device 4 can also comprise a filter element, not illustrated, for example, in the form of an interior filter.
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[0110] This means in particular that the clean air RL is not directly guided into the passenger compartment 3 but through the air conditioning device 4 into it. In this way, for example, it is possible to temperature-control the clean air RL from which CO.sub.2 and H.sub.2O has been removed. This means that a portion of the interior air IL is passed as raw air RO through the first sorption unit 6 and a further portion of the interior air IL is guided in recirculation operation through the air conditioning device 4. The device 5 as well as the air conditioning device 4 comprise their own blower devices 10, 12, 51 which however can be synchronized.
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[0112]
[0113] As illustrated in
[0114] The drive element 55 comprises in this context three switch positions. In a first switch position, only the second blower wheel 57 is driven, in a second switch position, both blower wheels 56, 57 are driven, and in a third switch position only the first blower wheel 56 is driven. Between the first blower wheel 56 and the drive element 55, a first coupling 59 can be provided that is suitable to couple the drive element 55 with the first blower wheel 56 or to decouple it from the drive element 55. Between the second blower wheel 57 and the drive element 55, a second coupling 60 can be provided that is suitable to couple the drive element 55 with the second blower wheel 57 or to decouple it from the drive element 55.
[0115] As illustrated in
[0116] As illustrated in
[0117] As illustrated in
[0118]
[0119] In a step S2, the other of the two sorption units 6, 7, for example, the second sorption unit 7, is switched by means of the air distribution device 19 into the desorption mode M2 in which, from the corresponding sorption unit 6, 7, carbon dioxide and water are desorbed into the supplied non-loaded regeneration air R1 and discharged into the environment U.
[0120] In a step S3, the steps S1 and S2 are performed alternately such that always one of the two sorption units 6, 7 is operated in the sorption mode M1 while the other one of the two sorption units 6, 7 is operated in the desorption mode M2.
[0121] In the hydraulic circuit diagrams of the motor vehicle 1 with device 5 for combined reduction of the carbon dioxide and water content in an enclosed air volume of
[0122] According to
[0123] This has advantages with respect to energy consumption because the heat quantity introduced once for regeneration is used optimally for desorption and heat losses are reduced thereby.
[0124] An alternative embodiment according to which also an at least partial recirculation of the at least partially loaded recirculation air R2, i.e., of the air volume flow which has passed at least once the sorption unit 6 which is in the desorption mode, is illustrated in
[0125] Accordingly, a throttle valve 501, in particular an adjustable throttle valve 501, is arranged in fluid communication between the outlet of the regeneration valve and the inlet of the recirculation conduit into the regeneration air conduit, by means of which the proportion of freshly supplied non-loaded regeneration air R1 can be adjusted. According to this embodiment, at the branch 401 no recirculation valve 500 is provided but the branch is embodied as a non-switched branch (e.g., distributor, T member, Y member or the like). This has the advantage that the desorption of the sorption unit which is in the desorption mode can always be realized at a sufficient concentration differential, which aids in reducing the total regeneration duration.
[0126] In
[0127]
[0128] Downstream of the first blower unit 10, a conduit 18 is provided which supplies the raw air RO to an air distribution device 19. The air distribution device 19 comprises a plurality of flap units 67, 68. Correspondingly, the air distribution device 19 can also be referred to as flap device or flap system. The flap units 67, 68 can be controlled by a common flap actuator 69. A first flap unit 67 can be brought selectively into fluid communication with the first sorption unit 6 or with the second sorption unit 7. Accordingly, a second flap unit 68 can also be moved selectively into fluid communication with the first sorption unit 6 or with the second sorption unit 7.
[0129] The conduit 18 is in fluid communication with the air distribution device 19 which, in turn, is in fluid communication with the two sorption units 6, 7. Depending on the switch position of the flap units 67, 68, the raw air RO can be supplied selectively either to the first sorption unit 6 or to the second sorption unit 7. In or at the conduit 18, a sensor 26, in particular a CO.sub.2, H.sub.2O and/or temperature sensor, can be provided.
[0130] A conduit 29 connects the air distribution device 19 with the passenger compartment 3. The conduit 29 can also comprise a sensor 30, in particular a CO.sub.2, H.sub.2O and/or temperature sensor. By means of the sensor 30, for example, it can be detected when the sorption unit 6, 7 which is in the sorption mode M1 is exhausted. Between the conduits 18, 29, a bypass conduit 31, in particular an adsorber bypass conduit, is provided for bypassing the sorption units 6, 7. Moreover, between the conduits 18, 29, a sensor 32, in particular a pressure sensor, is also provided which can detect a pressure difference between the conduits 18, 29.
[0131] The device 5 comprises a regeneration valve 36. The regeneration valve 36 is preferably a three-way valve. The ambient air UL is supplied as non-loaded regeneration air R1 to the regeneration valve 36. Moreover, the interior air IL as non-loaded regeneration air R1 can also be supplied via a conduit 37 to the regeneration valve 36. In or at the conduit 37, a check valve 35 is provided.
[0132] Via a conduit 40, loaded regeneration air R2 can be discharged to the environment U. The conduit 40 comprises a volume flow sensor 42. The volume flow sensor 42 can be referred to as desorption volume flow sensor. Downstream of the regeneration valve 36, a second blower device 12 is provided. In this context, the second blower device 12 is positioned at the pressure side, i.e., upstream of the sorption unit 6, 7. The second blower device 12 can also be provided at the suction side, i.e., downstream of the sorption units 6, 7. The second blower device 12 discharges the loaded regeneration air R2 into the environment U.
[0133] A volume flow sensor 41 can be arranged downstream of the first blower device 10. A volume flow sensor 42 is provided downstream of the air distribution device 19 in the conduit 40. Downstream of the second blower device 12, a further sensor 43, in particular a CO.sub.2, H.sub.2O and/or temperature sensor, is provided. Moreover, a further sensor 44, in particular a CO.sub.2, H.sub.2O and/or temperature sensor, is provided in or at the conduit 40. Moreover, a sensor 45 is provided that is suitable to detect a pressure difference between the conduit 40 and the air distribution device 19. The sensor 45 is provided downstream of the sensor 43.
[0134] Each sorption unit 6, 7 has associated therewith a sensor 46, 47, in particular a differential pressure sensor. A sensor 48, in particular as CO.sub.2, H.sub.2O and/or temperature sensor, can also be provided in the passenger compartment 3. In order to activate or deactivate the bypass conduit 31, a bypass valve 49 is provided. Each sorption unit 6, 7 comprises a plurality of temperature sensors 70, 71. For example, each sorption unit 6, 7 has correlated there with four such temperature sensors 70, 71. Each sorption unit 6, 7 can comprise a plurality of heating elements 11A, 11B, 13A, 13B. The heating elements 11A, 11B, 13A, 13B are optional. The heating elements 11A, 11B, respectively, 13A, 13B can be arranged in a sandwich-type arrangement. The device 5 comprises a further conduit 72, in particular a regeneration bypass conduit. The conduit 72 opens upstream of the volume flow sensor 42 into the conduit 40. By means of the conduit 72, the air distribution device 19 can be bypassed. The conduit 72 extends from a bypass valve 73 that is arranged downstream of the air distribution device 19 to the conduit 40.
[0135] Downstream of the bypass valve 73, i.e., between the bypass valve 73 and the air distribution device 19, an optional heating element 74, in particular a heat exchanger, is provided. By means of the heating element 74, for example, waste heat of an electric motor, of an internal combustion engine, or of a battery cooling system can be transmitted to the non-loaded regeneration air R1. Downstream of the heating element 74, an optional further heating element 75 is provided. The heating element 75 is arranged between the heating element 74 and the air distribution device 19. The heating element 75 is also suitable for transmitting heat to the non-loaded regeneration air R1. The heating element 75 can be, for example, an electrical heating element.
[0136]
[0137] As has been mentioned before, the first sorption unit 6 is in the desorption mode M2. For this purpose, by means of the regeneration valve 36 and the second blower device 12 non-loaded regeneration air R1 is taken in from the environment U. The non-loaded regeneration air R1 is then supplied to the heating element 74 that is embodied preferably as a heat exchanger and preheated. At the same time, the regeneration air R1 can be further heated by means of the optional heating element 75 that is arranged downstream of the heating element 74. By means of the first flap unit 67 of the air distribution device 19, the heated regeneration air R1 is supplied to the first sorption unit 6. Optionally, the first sorption unit 6 itself can also comprise heating elements 11A, 11B which are activated in the desorption mode M2. However, this is not mandatorily required. The second flap unit 68 is switched such that the loaded regeneration air R2 is discharged via the conduit 40 into the environment U.
[0138]
[0139] Since the heating element 74 and/or the heating element 75 are not integrated into the sorption units 6, 7 but in flow direction are arranged upstream thereof, namely, before inflow into the air distribution device 19, the heat introduction into the sorption units 6, 7 introduced by the air flow can be realized more homogeneously than in an in-situ heating via the electrical heating elements 11A, 11B, 13A, 13B in the sorption units 6, 7. Upon heating via the air flow, the heat transmission is realized mainly by convection, while upon heating by means of the heating elements a higher heat conduction proportion is present. By use of the external heating elements 74, 75, the desorption is realized faster. Moreover, the completion of the desorption mode M2 can be detected more easily with regard to measuring technology wherein the final criterion for the completion of the desorption is that the input temperature is identical to the output temperature. A further advantage is that only one heating element 74 or only one heating element 75 is required that can heat both sorption units 6, 7.
EMPLOYED REFERENCE CHARACTERS
[0140] 1 motor vehicle [0141] 2 car body [0142] 3 enclosed air volume/passenger compartment [0143] 4 air conditioning device [0144] 5 device [0145] 6 sorption unit [0146] 7 sorption unit [0147] 8 sorbent [0148] 9 sorbent [0149] 10 blower device [0150] 11 heating element [0151] 11A heating element [0152] 11B heating element [0153] 12 blower device [0154] 13 heating element [0155] 13A heating elements [0156] 13B heating element [0157] 14 conduit [0158] 15 conduit [0159] 16 conduit [0160] 17 conduit [0161] 18 conduit [0162] 19 air distribution device [0163] 20 valve [0164] 21 valve [0165] 22 valve [0166] 23 valve [0167] 24 conduit [0168] 25 conduit [0169] 26 sensor [0170] 27 conduit [0171] 28 conduit [0172] 29 conduit [0173] 30 sensor [0174] 31 bypass conduit [0175] 310 second bypass conduit [0176] 32 sensor [0177] 33 conduit [0178] 34 conduit [0179] 35 check valve [0180] 36 regeneration valve [0181] 360 regeneration air conduit [0182] 37 conduit [0183] 38 conduit [0184] 39 conduit [0185] 40 (desorption) conduit [0186] 401 branch of desorption conduit [0187] 41 volume flow sensor [0188] 42 volume flow sensor [0189] 43 sensor [0190] 44 sensor [0191] 45 sensor [0192] 46 sensor [0193] 48 sensor [0194] 49 bypass valve [0195] 490 second bypass valve [0196] 50 pressure sensor [0197] 500 recirculation valve [0198] 501 throttle valve, adjustable [0199] 510 recirculation conduit [0200] 51 blower device [0201] 52 valve [0202] 53 cooling element [0203] 54 heating element [0204] 55 drive element [0205] 56 blower wheel [0206] 57 blower wheel [0207] 58 arrow [0208] 59 coupling [0209] 60 coupling [0210] 61 gear wheel [0211] 62 gear wheel [0212] 63 cross shaft [0213] 64 cross shaft [0214] 65 coupling element [0215] 66 coupling element [0216] 67 flap unit [0217] 68 flap unit [0218] 69 flap actuator [0219] 70 temperature sensor [0220] 71 temperature sensor [0221] 72 conduit [0222] 73 bypass valve [0223] 74 heating element [0224] 75 heating element [0225] IL interior air [0226] M1 sorption mode [0227] M2 desorption mode [0228] RL clean air [0229] RO raw air [0230] R1 non-loaded regeneration air [0231] R2 loaded regeneration air [0232] S1 step [0233] S2 step [0234] S3 step [0235] U environment [0236] UL ambient air [0237] Q heat