EP3362741A1 - Method for obtaining energy from steam-containing vapor, and device for carrying out the method - Google Patents
Method for obtaining energy from steam-containing vapor, and device for carrying out the methodInfo
- Publication number
- EP3362741A1 EP3362741A1 EP16791318.5A EP16791318A EP3362741A1 EP 3362741 A1 EP3362741 A1 EP 3362741A1 EP 16791318 A EP16791318 A EP 16791318A EP 3362741 A1 EP3362741 A1 EP 3362741A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- steam
- condensation space
- swaths
- condensation
- cooling medium
- 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.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 51
- 238000009833 condensation Methods 0.000 claims abstract description 87
- 230000005494 condensation Effects 0.000 claims abstract description 87
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 61
- 239000002826 coolant Substances 0.000 claims description 30
- 239000007788 liquid Substances 0.000 claims description 22
- 238000011084 recovery Methods 0.000 claims description 17
- 238000005507 spraying Methods 0.000 claims description 12
- 238000000889 atomisation Methods 0.000 claims description 8
- 230000006835 compression Effects 0.000 claims description 7
- 238000007906 compression Methods 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 238000011144 upstream manufacturing Methods 0.000 claims description 6
- 238000001816 cooling Methods 0.000 claims description 5
- 238000005057 refrigeration Methods 0.000 claims description 5
- 230000005611 electricity Effects 0.000 claims description 4
- 238000010521 absorption reaction Methods 0.000 claims description 3
- 238000004891 communication Methods 0.000 claims description 3
- 238000010248 power generation Methods 0.000 claims 1
- 239000003570 air Substances 0.000 description 19
- 229920006395 saturated elastomer Polymers 0.000 description 12
- 239000003795 chemical substances by application Substances 0.000 description 8
- 238000001704 evaporation Methods 0.000 description 5
- 230000008020 evaporation Effects 0.000 description 5
- 239000002918 waste heat Substances 0.000 description 5
- 230000001419 dependent effect Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000011068 loading method Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 239000000654 additive Substances 0.000 description 3
- 239000000919 ceramic Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000009736 wetting Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 238000002604 ultrasonography Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000000443 aerosol Substances 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 230000002210 biocatalytic effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004422 calculation algorithm Methods 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 125000002524 organometallic group Chemical group 0.000 description 1
- 235000013606 potato chips Nutrition 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 230000001131 transforming effect Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24C—DOMESTIC STOVES OR RANGES ; DETAILS OF DOMESTIC STOVES OR RANGES, OF GENERAL APPLICATION
- F24C15/00—Details
- F24C15/20—Removing cooking fumes
- F24C15/2042—Devices for removing cooking fumes structurally associated with a cooking range e.g. downdraft
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24C—DOMESTIC STOVES OR RANGES ; DETAILS OF DOMESTIC STOVES OR RANGES, OF GENERAL APPLICATION
- F24C15/00—Details
- F24C15/32—Arrangements of ducts for hot gases, e.g. in or around baking ovens
- F24C15/322—Arrangements of ducts for hot gases, e.g. in or around baking ovens with forced circulation
- F24C15/327—Arrangements of ducts for hot gases, e.g. in or around baking ovens with forced circulation with air moisturising
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D21/0001—Recuperative heat exchangers
- F28D21/0014—Recuperative heat exchangers the heat being recuperated from waste air or from vapors
Definitions
- the present invention relates to a method for generating energy from steam containing steam according to claim 1 and an apparatus for carrying out this method according to claims 14-16.
- the atmosphere surrounding the food changes with regard to the enthalpy and composition of the substance mixture.
- the ambient air is enriched with water.
- the resulting air-vapor mixture for example in the case of baking steam, usually has a dew point between 50 ° C and 90 ° C, preferably between 60 ° C and 80 ° C, depending on the relative humidity.
- the temperature of the exhaust air is between 80 ° C and 150 ° C, depending on the process heat.
- the process air may contain, among other things, organic compounds, carbon, combustion gases, carbon dioxide and other substances.
- the resulting process air is called steam during baking and cooking processes. Accordingly, the baking in the baking chamber of the baking ovens in the baking chamber typically consist of water vapor, air and other organic constituents.
- the baking steam is condensed after leaving the baking space, for example by using a suitable cooling medium such as water or condensate, which is conducted in a suitable condensation space in countercurrent to the baking steam (WO 2012/1 1 3800 A1).
- a suitable cooling medium such as water or condensate
- the condensate temperature is between 60 ° C and 80 ° C.
- the resulting condensate can be removed via a heat exchanger, the heat energy, which is used for heating a medium, such as water, through the condensate located in the primary circuit.
- the temperature of the medium in the secondary circuit corresponds at most to the temperature of the condensate.
- the energy recovery is used here primarily the heating of service or drinking water.
- waste heat are sometimes generated in leakage currents, the full utilization of which far exceeds the required capacities, for example for hot water supply.
- heat losses for example, in the production of potato chips, heat losses of 5 MW / h are achieved.
- waste heat temperatures are required for specific technologies of heat utilization, which are usually above the normally occurring dew point of the vapor swaths.
- a method for energy recovery from steam containing steam, especially from baking steam, in steam-releasing systems, in particular baking systems (ovens) is provided.
- the dew point temperature ⁇ of the steam containing the steam is first increased to 95 to 99 ° C, preferably 95 to 97 ° C.
- the steam is condensed in at least one condensation space and the condensation condensate obtained after condensation of the steam is used for energy recovery / heat recovery.
- the dew point of the vapor swell can be increased to such an extent that the resulting swath condensate has waste heat temperatures which allow efficient use of the condensate even in the modern technologies of the absorption chiller and the ORC process
- the resulting condensate condensate after leaving the at least one condensation chamber has a temperature ⁇ between 95 ° C and 99 ° C, preferably between 95 ° C and 97 ° C and thus far above the usual condensate temperatures of steam, in particular baking steam of 65 ° C.
- the dew point temperature or dew point is that temperature of a mixture of a gaseous and a liquid medium in which the condensation and the evaporation process of the wet component are in equilibrium. In this case, the gas is saturated with steam or there is a 100 percent saturation. In this equilibrium state, the vapor partial pressure is equal to the saturation vapor pressure of water.
- the dew point temperature is essentially dependent on the water load X of the vapor swath, as well as the present pressure p.
- the relationship between these two parameters and the dew point temperature ⁇ is described by the Magnus formula for describing the saturation vapor pressure of water.
- equations (1) and (2) can be equated and resolved according to the temperature ⁇ , giving the formula for describing the dew point temperature ⁇ as a function of the water load X and the present pressure p.
- a dew point temperature of 95 ° to 99 ° C. can be set correspondingly by varying the vapor pressure p as well as the water loading X.
- the steam containing the water vapor is compressed or compressed for the purpose of increasing the dew point temperature T.
- the pressure level of the windrows is increased by compression of the moist air.
- the pressure required for the compression depends on the initial temperature of the windrow and the dew-point temperature to be achieved and is given by the following equation (4).
- the steam contained in the steam is adjusted to a pressure p before the steam enters the condensation space is compressed, so that a dew point temperature ⁇ between 95 and 99 ° C, preferably 95 and 97 ° C is reached.
- the compression of the swath e.g. the baking steam left the oven, before entering the steam into the condensation space using a compressor or compressor.
- At least one liquid, in particular water or condensate is sprayed into the steam before entering the condensation space. This increases the moisture content in the windrow.
- the at least one liquid is atomized before entry into the swath.
- atomizing the liquid is decomposed into droplets in the nanometer and micrometer range, in particular, the available surface of the liquid is increased.
- This atomization of the liquid in the swaths can be done by ultrasonic atomization or by using piezo-controlled nozzles in the swaths.
- the liquid is atomized microscopically fine.
- the liquid medium is supplied with a pre-pressure of 1 -3 bar in the atomizer.
- the sonic gas eg air or exhaust air
- the sonic gas is excited to a vibration of 18 to 30 kHz.
- Another variant of the atomization represents the possibility of spraying water or condensate with piezo-driven nozzles or piezo-driven aerosol generators.
- a further energy enrichment by the application of a microwave voltage This further breaks up molecular clusters and increases the rate of drying.
- the change in the water load can be determined by the following equation (5), which is obtained by changing from equation (4):
- Humidifying the steam with water causes the moist air stream to cool down considerably. This is due to the difference in temperature between the hot humid air and the sprayed water, especially the fact that the heat of evaporation of the water must be supplied by the humid air. For this reason, the energy accumulation or the energy input by spraying or atomizing the liquid such as water in the windrows, for example by means of ultrasound is necessary to counteract the loss of energy.
- the amount of liquid to be sprayed in the swath depends on the initial moisture content of the swath and is determined and controlled by the dew point temperature to be reached. The determination of the réellestauainss and the desired dew point can be done for example by means of suitable sensors and the amount of liquid to be sprayed is controlled by a corresponding nozzle.
- the production of the water vapor required for this purpose can be done in a large-scale water boiler, high-speed steam generators, clean steam generators, electrically heated steam generators or heat carrier heater.
- a forced-circulation boiler is used as a high-speed steam generator.
- a continuous flow of water pipe coil is heated by a burner flame and the resulting flue gases in the countercurrent principle.
- Fuel and water are regulated so that wet steam with low residual water content is formed.
- a water separator it is possible to obtain saturated steam conditions.
- the advantage of using a forced-circulation boiler is the small footprint and the quick adaptation to load changes.
- the amount of steam to be introduced in the steam is also in this case dependent on the initial moisture of the windrow and is to be reached by the Dew point temperature determined and controlled. For example, by introducing 2.5 kwh / kg (dry) air, it is possible to increase the dew point temperature of a windrow by 20 ° C.
- the condensation of the swaths with increased dew point temperature ⁇ takes place by contacting the swaths in countercurrent with at least one cooling medium in the at least one condensation space.
- water or steam condensate is preferably used, which is passed after cooling and passage through a heat exchanger back into the system.
- the at least one cooling medium is at a flow rate between 0.5 m / min and 10 m / min, preferably between 1, 0 m / min and 5.0 m / min, more preferably between 1, 0 m / min and 2.5 m / min passed through the at least one condensation chamber.
- the cooling medium accordingly flows into the condensation space in the form of a liquid flow, in particular a continuous liquid flow. There is no spray condensation and thus no droplet formation of the incoming cooling medium in the condensation chamber.
- a spray condensation would not be feasible in the present process, since the swaths enter the condensation space with high flow velocity and thus the spray droplets instead of a filler to be entrained by the air flow, so that a reduced cleaning effect and a deteriorated energy utilization or worse Heat recovery occurs.
- the cooling medium such as water or steam condensate
- a suitable surface tension reducing additive e.g. Surfactants or emulsifiers, which cause a better wetting of the ceramic surface.
- the steam condensate obtained with the present process can be used as hot water via a heat exchanger, optionally after prior purification or filtration, in particular for the supply of hot water heating.
- the obtained Schwadenkondensat can be converted into at least one heat exchanger for heat recovery.
- ORC Organic Rankine Cycle
- the resulting windrow condensate can be used for cooling in absorption refrigeration plants.
- the present method is carried out in one of the following devices.
- such a device comprises at least one horizontally and / or vertically arranged condensation space with at least one inlet for the entry of the steam containing steam and at least one outlet for the outlet of the condensed steam and at least one input for at least one cooling medium and at least one Output for the at least one cooling medium, wherein the respective inputs and outputs are arranged to each other such that steam and cooling medium flow through the condensation space in countercurrent, and at least one compressor for compressing the entering into the condensation space of water vapor contained swaths, wherein the at least one compressor along the supply line of the swaths upstream of the entrance for the entry of water vapor contained swaths is provided in the condensation space.
- such a device comprises at least one horizontally and / or vertically arranged condensation space with at least one inlet for the entry of steam containing steam and at least one outlet for the outlet of the condensed steam and at least one input for at least one cooling medium and at least one Output for the at least one cooling medium, wherein the respective inputs and outputs are arranged in such a way that swaths and cooling medium flow through the condensation space in countercurrent, and at least one device for spraying at least one liquid in the water vapor contained in the condensation chamber swaths, wherein the at least one device for spraying along the inlet of the swaths upstream of the inlet for the entry of steam containing steam is provided in the condensation space.
- such a device comprises at least one horizontally and / or vertically arranged condensation chamber with at least one inlet for the entry of the steam containing steam and at least one outlet for the outlet of the condensed steam and at least one input for at least one cooling medium and at least an outlet for the at least one cooling medium, wherein the respective inlets and outlets are arranged in such a way that steam and cooling medium flow through the condensation space in countercurrent, and at least one steam generator for introducing steam into the steam contained in the condensation space, wherein the at least a steam generator along the supply of the steam upstream of the entrance for the entry of water vapor contained steam is provided in the condensation space.
- the condensation of the swaths takes place on at least one surface of a condensing agent arranged in the condensation space.
- the at least one condensation agent is arranged in the condensation space such that it is at least temporarily contacted or moistened by the cooling medium. Due to this at least temporarily taking place wetting of the surface of the condensing agent with the coolant also eliminates the Necessity of washing the same, since possibly condensed or separated organic substances are dissolved directly in the swirl condensate.
- An essential aspect is that the surface of the condensing agent does not dry, otherwise there will be too difficult to remove encrustations on the surface of the condensing agent.
- the at least one surface of the condensing agent arranged in the condensation space can have a cavity structure, in particular an open-cell system, a structured packing and / or an unstructured packing. It is also possible to provide or coat the condensing agents with organometallic or biocatalytic surfaces,
- the open cell cell system used as condensing agent is in the form of a ceramic pore system with a pore size of 20 ppi, preferably 15 ppi, more preferably 10 ppi.
- a ceramic pore system with a pore size of 20 ppi, preferably 15 ppi, more preferably 10 ppi.
- the use of ceramic foam with a corresponding pore size conceivable, this about 20% of the free cross-section of the condensation space, the e.g. is formed in the form of a column or a tube claimed.
- the at least one condensation space communicates with at least one heat exchange facility, through which the swirl condensate formed in the condensation space is guided.
- the at least one condensation space may also be in communication with at least one ORC (Organic Rankine Cycle) installation in which the steam condensate formed in the condensation space is used to generate electricity.
- ORC Organic Rankine Cycle
- the at least one condensation space communicates with at least one apparatus for generating refrigeration in which the steam condensate formed in the condensation space is used for refrigeration.
- Figure 1 is a schematic representation of an apparatus for performing the present method according to a first embodiment
- Figure 2 is a schematic representation of an apparatus for carrying out the present method according to a second embodiment
- FIG. 3 shows a schematic illustration of an apparatus for carrying out the present method according to a third embodiment.
- FIG. 1 shows a schematic representation of the heat recovery by means of increasing the dew point temperature of the windrow by moistening the windrow with a liquid, in particular with a condensate.
- baking steam or steam is introduced through a conduit 2 in a condensation chamber 3.
- liquid is sprayed into the baking swath using a suitable spraying device 4a, in particular by means of ultrasonic atomization.
- the amount of liquid to be sprayed in the swath depends on the initial moisture content of the swath and is determined and controlled by the dew point temperature to be reached.
- the output dew point TP1 of the windrow before the spraying device 4a is determined.
- the amount of liquid to be fed by the spraying device 4a is regulated.
- the condensation of the moistened baking steam is carried out using a cooled condensate in countercurrent.
- Embodiment 2 Humidification of the windrow with saturated steam
- Figure 2 shows a schematic representation of the heat recovery by increasing the dew point temperature of the windrow by wetting the wind with saturated steam.
- baking steam or steam is introduced through a conduit 2 in a condensation chamber 3.
- saturated steam is introduced into the baking steam.
- the necessary saturated steam is generated in a suitable steam generator 4b, in particular a high-speed steam generator.
- the amount of saturated steam to be introduced into the windrows is also dependent on the initial moisture content of the windrow and is determined and controlled by the dew point temperature to be achieved.
- the minutiacity of TP1 of the windrow is determined before introducing the saturated steam.
- the amount of saturated steam to be introduced in the windrows is regulated.
- the condensation of the moistened baking steam is carried out using a cooled condensate in countercurrent.
- the condensate leaving the condensation chamber is fed to a heat exchanger 5 for heat recovery,
- Embodiment 3 Compression of the windrow
- FIG. 3 shows a schematic representation of the heat recovery by means of increasing the dew point temperature of the wind through compression of the windrow.
- baking steam or steam is introduced through a conduit 2 in a condensation chamber 3.
- the baking steam is compressed.
- the pressure increase or compression of the baking steam is done using a suitable compressor or compressor 4c.
- a pressure increase of 150 kPa (1, 5 bar) leads to an increase in the dew point of 75 ° C to 95 ° C.
- the condensation of the moistened baking steam is carried out using a cooled condensate in countercurrent.
- the condensate leaving the condensation chamber is fed to a heat exchanger 5 for heat recovery,
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
- Drying Of Solid Materials (AREA)
Abstract
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL16791318T PL3362741T3 (en) | 2015-10-16 | 2016-10-11 | Method for obtaining energy from steam-containing vapor, and device for carrying out the method |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102015220221.6A DE102015220221A1 (en) | 2015-10-16 | 2015-10-16 | Process for the production of energy from steam containing steam and apparatus for carrying out this process |
PCT/EP2016/074295 WO2017064036A1 (en) | 2015-10-16 | 2016-10-11 | Method for obtaining energy from steam-containing vapor, and device for carrying out the method |
Publications (2)
Publication Number | Publication Date |
---|---|
EP3362741A1 true EP3362741A1 (en) | 2018-08-22 |
EP3362741B1 EP3362741B1 (en) | 2021-04-14 |
Family
ID=57241048
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP16791318.5A Active EP3362741B1 (en) | 2015-10-16 | 2016-10-11 | Method for obtaining energy from steam-containing vapor, and device for carrying out the method |
Country Status (5)
Country | Link |
---|---|
EP (1) | EP3362741B1 (en) |
DE (1) | DE102015220221A1 (en) |
DK (1) | DK3362741T3 (en) |
PL (1) | PL3362741T3 (en) |
WO (1) | WO2017064036A1 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP4069665B1 (en) * | 2019-12-02 | 2024-08-07 | Services Pétroliers Schlumberger | Reducing energy consumption in meg reclamation |
CN110894968A (en) * | 2019-12-11 | 2020-03-20 | 真美妙(上海)餐饮管理有限公司 | Oil fume extraction system used on catering pot body |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3013330A1 (en) * | 1980-04-05 | 1981-10-08 | Fr. Winkler KG Spezialfabrik für Bäckereimaschinen und Backöfen, 7730 Villingen-Schwenningen | Baking vapours waste heat recovery - by heat exchanger in first and by recycling to steam zone in second zone |
DE102009014805A1 (en) * | 2009-03-25 | 2010-09-30 | Pietruska, Michael | Energy recovery system for use in system of baking oven operated with gas- or oil burners, has heat exchanger chamber provided with inlet for oven waste gas or fumes, and cleaning chamber provided with outlet connected to chimney |
DE102011004460A1 (en) | 2011-02-21 | 2012-08-23 | Kuchenmeister Gmbh | Process for the removal of swathes containing organic ingredients and their conversion products and for heat recovery from swaths and an apparatus for performing this method |
DE102012211862A1 (en) * | 2012-07-06 | 2014-01-09 | Siemens Aktiengesellschaft | Process for the production of water from the exhaust gas stream of a gas turbine plant |
-
2015
- 2015-10-16 DE DE102015220221.6A patent/DE102015220221A1/en not_active Ceased
-
2016
- 2016-10-11 PL PL16791318T patent/PL3362741T3/en unknown
- 2016-10-11 EP EP16791318.5A patent/EP3362741B1/en active Active
- 2016-10-11 WO PCT/EP2016/074295 patent/WO2017064036A1/en active Application Filing
- 2016-10-11 DK DK16791318.5T patent/DK3362741T3/en active
Also Published As
Publication number | Publication date |
---|---|
EP3362741B1 (en) | 2021-04-14 |
WO2017064036A1 (en) | 2017-04-20 |
DK3362741T3 (en) | 2021-07-12 |
PL3362741T3 (en) | 2021-12-06 |
DE102015220221A1 (en) | 2017-04-20 |
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