EP3748257B1 - Vorrichtung zur sicheren durchführung eines linksdrehenden thermodynamischen kreisprozesses mittels eines entzündlichen arbeitsfluids mit der verwendung von fluidadsoprtion - Google Patents
Vorrichtung zur sicheren durchführung eines linksdrehenden thermodynamischen kreisprozesses mittels eines entzündlichen arbeitsfluids mit der verwendung von fluidadsoprtion Download PDFInfo
- Publication number
- EP3748257B1 EP3748257B1 EP20171754.3A EP20171754A EP3748257B1 EP 3748257 B1 EP3748257 B1 EP 3748257B1 EP 20171754 A EP20171754 A EP 20171754A EP 3748257 B1 EP3748257 B1 EP 3748257B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- working fluid
- housing part
- interspace
- gas
- adsorbent
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000012530 fluid Substances 0.000 title claims description 59
- 238000000034 method Methods 0.000 title claims description 15
- 239000003463 adsorbent Substances 0.000 claims description 24
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 11
- 238000001179 sorption measurement Methods 0.000 claims description 10
- 239000011230 binding agent Substances 0.000 claims description 8
- 239000008188 pellet Substances 0.000 claims description 4
- 230000000694 effects Effects 0.000 claims description 2
- 238000005516 engineering process Methods 0.000 claims description 2
- 239000008187 granular material Substances 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 claims 3
- 230000002040 relaxant effect Effects 0.000 claims 1
- 239000003570 air Substances 0.000 description 21
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 20
- 239000007789 gas Substances 0.000 description 18
- 239000003507 refrigerant Substances 0.000 description 11
- 238000005057 refrigeration Methods 0.000 description 11
- 239000001294 propane Substances 0.000 description 10
- 239000000126 substance Substances 0.000 description 7
- 238000013461 design Methods 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 4
- 239000002594 sorbent Substances 0.000 description 4
- 238000012546 transfer Methods 0.000 description 4
- 238000009423 ventilation Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000004378 air conditioning Methods 0.000 description 3
- 125000004122 cyclic group Chemical group 0.000 description 3
- 238000004880 explosion Methods 0.000 description 3
- RAXXELZNTBOGNW-UHFFFAOYSA-N imidazole Natural products C1=CNC=N1 RAXXELZNTBOGNW-UHFFFAOYSA-N 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 231100000331 toxic Toxicity 0.000 description 3
- 230000002588 toxic effect Effects 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 241001295925 Gegenes Species 0.000 description 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N Propene Chemical compound CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 2
- 239000012267 brine Substances 0.000 description 2
- 239000002775 capsule Substances 0.000 description 2
- 230000006835 compression Effects 0.000 description 2
- 238000007906 compression Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 2
- 241001136792 Alle Species 0.000 description 1
- 238000006424 Flood reaction Methods 0.000 description 1
- 206010019233 Headaches Diseases 0.000 description 1
- 206010028813 Nausea Diseases 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000003745 diagnosis Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 238000009499 grossing Methods 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 231100000869 headache Toxicity 0.000 description 1
- 238000005338 heat storage Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000003533 narcotic effect Effects 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000008693 nausea Effects 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 235000021317 phosphate Nutrition 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 230000009182 swimming Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 230000007306 turnover Effects 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
Images
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B25/00—Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00
- F25B25/005—Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00 using primary and secondary systems
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2339/00—Details of evaporators; Details of condensers
- F25B2339/04—Details of condensers
- F25B2339/047—Water-cooled condensers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2400/00—General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
- F25B2400/12—Inflammable refrigerants
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B2500/00—Problems to be solved
- F25B2500/22—Preventing, detecting or repairing leaks of refrigeration fluids
Definitions
- the invention relates to irregular states in refrigeration circuits in which a working fluid acting as a refrigerant is circulated in a thermodynamic cycle, such as the Clausius-Rankine cycle.
- thermodynamic cycle such as the Clausius-Rankine cycle.
- These are mainly heat pumps, air conditioning systems and refrigerators, as they are common in residential buildings.
- Residential buildings are private houses, apartment building complexes, hospitals, hotel complexes, gastronomy and combined residential and commercial buildings in which people live and work permanently, in contrast to mobile devices such as car air conditioning systems or transport boxes, or industrial systems or medical devices. What these cycle processes have in common is that they generate useful heat or cold using energy and form heat transfer systems.
- thermodynamic cycle processes used have been known for a long time, as have the safety problems that can arise when using suitable working fluids. Aside from water, the most common working fluids of the time were flammable and toxic. In the last century they led to the development of safety refrigerants, which consisted of fluorinated hydrocarbons. However, it turned out that these safety refrigerants damage the ozone layer, lead to global warming, and that their safety-related harmlessness led to design carelessness. Up to 70% of the turnover was accounted for by the need to refill leaking systems and their leakage losses, which was accepted as long as this was felt to be economically justifiable in individual cases and promoted the need for replacement purchases.
- Propane is also heavier than air, so it sinks to the floor in still air and accumulates there, but after a certain time it mixes with the room air, which also depends on the leakage rate and room height. If part of the propane collects under very unfavorable conditions in a low-flow zone of the closed room in which the malfunctioning unit is located, the local explosion limits can be reached much more quickly than would be expected from the quotient of the total room volume to the amount of propane that has escaped.
- the WO 2015/032905 A1 seeks to solve this problem by a generator for electric power in the opening or locking this space is integrated and when it is actuated in a first step generates and provides the electrical energy with which the sensor is activated, and in the event of an alarm, the Locking then does not release, but causes the closed room to be ventilated, and only allows unlocking and opening in a second step.
- the DE 10 2011 116 863 A1 describes a method for securing a device for a thermodynamic cycle process, which is operated with a process fluid, that contains or consists of at least one environmentally hazardous, toxic and/or flammable substance.
- a process fluid that contains or consists of at least one environmentally hazardous, toxic and/or flammable substance.
- an adsorbent is brought into contact with the process fluid, in particular ammonia, propane or propene, and the substance is selectively bound by the adsorbent.
- the adsorbent is regenerated after use.
- Zeolite also in combination with imidazole or phosphates, and also CuBTC are proposed as adsorbents; the adsorbent can be in the form of a bed, a shaped body, a paint, a spray film or a coating.
- the support structure of the shaped body can consist of a microstructure, lamellar structure, tube bundle, tube register and sheet metal and must be mechanically stable and greatly increase the surface area.
- the potentially contaminated air is usually circulated continuously, but it can also be initiated by a sensor that switches on the ventilation after a threshold value has been reached or if an accident is detected.
- the adsorption can be carried out inside or outside a closed space.
- the DE 195 25 064 C1 describes a refrigeration machine with a gas-tight housing, which accommodates all refrigerant-carrying components of the machine, a space connecting the interior of the gas-tight housing with an outlet is provided, and the space is filled with a refrigerant-sorbing substance.
- the amount of sorbing substance is dimensioned in such a way that the entire amount of refrigerant that may escape can be absorbed and kept away from the environment.
- the space filled with the sorbing substance is open to the environment. For heavier-than-air refrigerants, the space is open at the bottom, for lighter-than-air ones, it is open at the top, so a conveying fan is not required.
- the sorbent is introduced into the housing and completely encloses the refrigeration machine or the refrigerant-carrying equipment. Baffles are provided on its way out to prevent shunt flows and force escaping gas through the sorbent. Also one double-walled embodiment, in which the sorbent is arranged in the double jacket, is possible.
- a measuring device for refrigerant can be provided at the outlet of the space filled with the sorbing substance to the environment.
- the EP 3 106 780 A1 describes a heat pump system housed in an airtight enclosure lined with a binder.
- An adsorption unit with forced ventilation can be arranged within this housing, which cleans the air in the housing in the air recirculation mode.
- This air recirculation mode can take place continuously or only in the event of a fault or at regular intervals.
- An ignition burner, a pilot flame, a catalytic burner or a heating wire can also be arranged downstream of this sorption stage, which burns any remaining combustible impurities.
- a supply of fresh air in connection with the discharge of cleaned exhaust air is also conceivable.
- a binder be it an adsorbent or a chemical binder
- a binder should be able to absorb all of the working fluid even at low partial pressures. This is best done in a slow flow through a finely distributed medium.
- a large quantity of working fluid is released under high pressure in a very short time, which suddenly puts the mostly pressure-tight housing under pressure. Tests resulted in peak pressure values of up to 25 hPa, which would lead to deformation of typical designs and the subsequent escape of working fluid.
- the object of the invention is therefore to provide an improved device which better solves the problems presented, including the conflicting objectives, and no longer has the disadvantages.
- a Clausius-Rankine process which is operated with R290, serves as a left-handed cyclic process.
- the adsorbent activated carbon is preferably used as the binder. All gaseous or liquid media with which heat is transferred are to be understood here as heat transfer fluids, ie air, water, brine, heat transfer oils or the like.
- the nesting of the two housing parts can be done in different ways.
- the outer housing part can be fitted onto the lower, inner housing part from above, with the underside of the outer housing part being completely open.
- the aggregates of the cyclic process are then all arranged in the inner housing part and the connections are made below and do not pierce the outer housing part.
- the outer housing part can also be arranged below and form a kind of trough for the inner housing part, with the inner housing part being placed on top.
- the aggregates of the cyclic process are then all arranged in the outer housing part, the connections are made below and do not pierce the inner housing part.
- the outer housing part can also be pushed laterally over the inner housing part.
- one housing part is always fixed and the other is movable along an axis, with this movement being guided by suitable mounting in order to prevent tilting. If an overpressure event occurs, the overpressure causes the movable housing part to move due to this pressure and opens the way to the gap between the two housing parts.
- An adsorbent is arranged in this intermediate space, which is preferably a bed with low flow resistance.
- rounded channels and flow straighteners are preferably provided so that a homogeneous gas flow is created.
- a limit stop is preferably provided in order to limit the movement of the movable housing part.
- the movable housing part is mounted on a shaped body or a bed of adsorbent which, in the event of small leaks, causes the working fluid that has escaped to be bound without the gas path into the intermediate space being opened up. In this way, there is a different treatment of occasional small and very rare large leakage events.
- the intermediate space between the two housing parts is provided on 4 sides.
- a high flow cross section can be achieved with a large smoothing effect.
- the pressure at which the gas path should open into the intermediate space can be defined by the weight of the moving housing part. However, if this does not fit, springs can compensate for the required difference.
- elements such as retaining screens, bases and assembly aids or the like can also be used in the usual way and the two housing parts can also have covers, removable side parts, service openings, safety valves and the like for assembly purposes.
- Fig. 1a shows a first embodiment variant in the closed state using a schematic diagram of a refrigeration circuit 1 with a compressor 2, a condenser 3, a pressure reduction 4 and an evaporator 5 in a closed housing, which is formed from an inner housing part 6 and an outer housing part 11.
- the inner housing part 6 is open at the bottom and closed at the top, while the outer housing part 11 is open at the top and closed at the bottom.
- the inner housing part 6 rests in the outer housing part 11 like a trough.
- the housing has a heat source connection 7, a heat source flow 8, a heat sink flow 9 and a heat sink connection 10.
- the refrigeration circuit 1 is filled with the flammable working fluid propane, which is also known under the designation R290. operated.
- Fig. 1b shows the first variant in the open state after a sudden significant leakage event.
- the pressure inside the inner housing part 6 increases so quickly that the adsorbent layer cannot absorb the escaping working fluid quickly enough. Due to the increase in pressure, the inner housing part 6 is lifted until the inner pressure and the weight of the inner housing part 6 are in equilibrium.
- the gas which consists of a mixture of working fluid and air, enters the intermediate space 12 through the passage opening 14 at the bottom. where it is directed upwards through another adsorption layer, which offers only a very low flow resistance. Most of the working fluid is adsorbed therein. A small residual flow exits through the passage opening 15 into the environment. After the end of the overpressure event, the inner housing part 6 moves back into its starting position. The loaded adsorbent is then professionally removed.
- Figure 2a shows an alternative embodiment in the closed state, the main difference from the first variant being that the inner housing part 6 is not inserted in the outer housing part 11 like in a trough, but that the outer housing part 11 is arranged over the inner housing part 6 like a hat. Otherwise the structure is analogous.
- Figure 2b shows the alternative embodiment in the open state.
- the outer housing part is lifted by the resulting overpressure and releases a passage opening 14 which, in contrast to the first embodiment variant, is arranged at the top. Due to the increase in pressure, the outer housing part 11 is lifted until the internal pressure and the weight of the housing part 11 are in equilibrium.
- the gas which consists of a mixture of working fluid and air, enters the intermediate space 12 through the through-opening 14 at the top, where it is passed downwards through another adsorption layer, which offers only a very low flow resistance. Most of the working fluid is adsorbed therein. A small residual flow exits through the passage opening 15 into the environment. After the end of the overpressure event, the outer housing part 11 moves back to its starting position. The loaded adsorbent is then professionally removed.
- the outer housing part 11 encloses the inner housing part 6 and forms a circumferential space 12 in which the adsorbent is placed.
- the adsorbent is preferably attached in a detachable manner to the non-moving housing part.
- the circumferential intermediate space can also be formed from a number of compartments, for example one on each of the outsides, which makes it easier to detach them after loading.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Separation Of Gases By Adsorption (AREA)
- Electrical Discharge Machining, Electrochemical Machining, And Combined Machining (AREA)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
HRP20221496TT HRP20221496T1 (hr) | 2019-06-03 | 2020-04-28 | Uređaj za sigurno provođenje lijevokretnog termodinamičkog kružnog procesa uz pomoć zapaljivog radnog fluida uz upotrebu adsorpcije fluida |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102019114744.1A DE102019114744A1 (de) | 2019-06-03 | 2019-06-03 | Fluidadsorption |
Publications (2)
Publication Number | Publication Date |
---|---|
EP3748257A1 EP3748257A1 (de) | 2020-12-09 |
EP3748257B1 true EP3748257B1 (de) | 2022-10-19 |
Family
ID=70475985
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP20171754.3A Active EP3748257B1 (de) | 2019-06-03 | 2020-04-28 | Vorrichtung zur sicheren durchführung eines linksdrehenden thermodynamischen kreisprozesses mittels eines entzündlichen arbeitsfluids mit der verwendung von fluidadsoprtion |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP3748257B1 (es) |
DE (1) | DE102019114744A1 (es) |
DK (1) | DK3748257T3 (es) |
ES (1) | ES2933612T3 (es) |
FI (1) | FI3748257T3 (es) |
HR (1) | HRP20221496T1 (es) |
PL (1) | PL3748257T3 (es) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP4382193A1 (de) * | 2022-12-09 | 2024-06-12 | Vaillant GmbH | Adsorptionsvorrichtung |
EP4382192A1 (de) * | 2022-12-09 | 2024-06-12 | Vaillant GmbH | Adsorberpartitionierung |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102022100269A1 (de) | 2022-01-07 | 2023-07-13 | Vaillant Gmbh | Katalytische Abluftbehandlung für eine Wärmepumpe |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE553295C (de) | 1931-02-03 | 1932-06-23 | Bbc Brown Boveri & Cie | Gekapselte Kompressionskaeltemaschine |
DE19525064C1 (de) | 1995-07-10 | 1996-08-01 | Joachim Dr Ing Paul | Kältemaschine |
DE10352957B3 (de) * | 2003-11-13 | 2005-02-03 | Audi Ag | Klimaanlage für Kraftfahrzeuge |
DE102011116863A1 (de) | 2011-10-25 | 2013-04-25 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Verfahren zur Sicherung einer Vorrichtung für einen thermodynamischen Kreisprozess und abgesicherte Vorrichtung für einen thermodynamischen Kreisprozess |
WO2015032905A1 (de) | 2013-09-05 | 2015-03-12 | Holger König | Verfahren zur verhinderung einer leckage aus einem behälter und ein behälter mit leckagesicherung |
EP3106780B1 (de) | 2015-06-17 | 2017-11-22 | Vaillant GmbH | Wärmepumpenanlage |
DE102017126947A1 (de) * | 2017-11-16 | 2019-05-16 | Vaillant Gmbh | Fluidadsorption mit Inertgasverdrängung |
-
2019
- 2019-06-03 DE DE102019114744.1A patent/DE102019114744A1/de active Pending
-
2020
- 2020-04-28 HR HRP20221496TT patent/HRP20221496T1/hr unknown
- 2020-04-28 ES ES20171754T patent/ES2933612T3/es active Active
- 2020-04-28 FI FIEP20171754.3T patent/FI3748257T3/de active
- 2020-04-28 EP EP20171754.3A patent/EP3748257B1/de active Active
- 2020-04-28 PL PL20171754.3T patent/PL3748257T3/pl unknown
- 2020-04-28 DK DK20171754.3T patent/DK3748257T3/da active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP4382193A1 (de) * | 2022-12-09 | 2024-06-12 | Vaillant GmbH | Adsorptionsvorrichtung |
EP4382192A1 (de) * | 2022-12-09 | 2024-06-12 | Vaillant GmbH | Adsorberpartitionierung |
Also Published As
Publication number | Publication date |
---|---|
PL3748257T3 (pl) | 2023-01-30 |
ES2933612T3 (es) | 2023-02-10 |
FI3748257T3 (en) | 2023-01-13 |
HRP20221496T1 (hr) | 2023-02-17 |
EP3748257A1 (de) | 2020-12-09 |
DE102019114744A1 (de) | 2020-12-03 |
DK3748257T3 (da) | 2022-12-19 |
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