EP3164656A1 - Block-in-shell wärmeübertrager - Google Patents
Block-in-shell wärmeübertragerInfo
- Publication number
- EP3164656A1 EP3164656A1 EP15731255.4A EP15731255A EP3164656A1 EP 3164656 A1 EP3164656 A1 EP 3164656A1 EP 15731255 A EP15731255 A EP 15731255A EP 3164656 A1 EP3164656 A1 EP 3164656A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- collector
- heat exchanger
- pipe
- medium
- jacket
- 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.)
- Withdrawn
Links
Classifications
-
- 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
- F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D9/0006—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the plate-like or laminated conduits being enclosed within a pressure vessel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F21/00—Constructions of heat-exchange apparatus characterised by the selection of particular materials
- F28F21/08—Constructions of heat-exchange apparatus characterised by the selection of particular materials of metal
- F28F21/081—Heat exchange elements made from metals or metal alloys
- F28F21/084—Heat exchange elements made from metals or metal alloys from aluminium or aluminium alloys
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/007—Auxiliary supports for elements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/007—Auxiliary supports for elements
- F28F9/013—Auxiliary supports for elements for tubes or tube-assemblies
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/026—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits
- F28F9/027—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes
- F28F9/0275—Header boxes; End plates with static flow control means, e.g. with means for uniformly distributing heat exchange media into conduits in the form of distribution pipes with multiple branch pipes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2275/00—Fastening; Joining
- F28F2275/04—Fastening; Joining by brazing
Definitions
- the invention relates to a heat exchanger according to claim 1.
- a heat exchanger is used for indirect heat transfer between a first and a second medium and has a jacket which surrounds a jacket space for receiving the first medium, and arranged in the shell space plate heat exchanger having a heat exchanger block comprising first heat transfer passages for receiving the first medium and second heat transfer passages for receiving the second medium, wherein the heat transfer passages are configured so that heat of a second medium flowing into the second heat transfer passages is indirectly transferable to first medium flowing into the first heat transfer passages.
- the heat exchanger has a first collector (also referred to as a header), which is fixed to a first side of the heat exchanger block and is in fluid communication with the second heat transfer passages, so that the second medium via the first collector in the second
- Heat transfer passages can be introduced, and a second collector (or header), on one of the first side facing away from the second side of the
- Heat exchanger block is set and with the second
- Heat transfer passages is in fluid communication, so that the second medium is removable via the second collector from the second heat transfer passages.
- a heat exchanger is shown, for example, in "The Standards of the brazed aluminum plate-fin heat exchanger manufacturer's association (ALPEMA)", third edition, 2010, page 67 in Figure 9-1, which shows a jacket ("Shell” or “Kettle "), which encloses a mantle space, and at least one in the
- Sheath space arranged plate heat exchanger (“core” or “block”). Such a design of a heat exchanger is therefore also called “core-in-shell” - or
- the present invention seeks to provide a block-in-shell heat exchanger of the type mentioned, which allows a shortening of the axial length of the shell.
- Extension direction along the second side extends, wherein a along the extension direction extending first pipe, which is preferably aligned with the second collector, for withdrawing the second medium from the second collector in fluid communication with the second collector and in the extension direction through a passage opening of the shell of the Jacket space of the heat exchanger is led out.
- the extension direction is at a
- the heat exchanger block can be moved in the direction of
- Longitudinal axis be made shorter overall. Accordingly, the sheath or kettlebell can be shorter in the direction of the longitudinal axis.
- the first collector extends along the extension direction along the first side, wherein at least one connected to the first collector first inlet port is provided, which extends transversely to the extension direction of the first collector, wherein the second medium via the first inlet port in the first collector can be introduced, and wherein the
- Heat exchanger has a arranged in the shell space third collector, which is in fluid communication with the at least one inlet port, wherein
- Pipe for withdrawing the second medium from the second collector in fluid communication with the second collector and counter to the direction of extension through a further passage opening of the shell of the shell space
- the first and the further first pipeline are aligned with each other and depart from mutually remote sides of the second collector.
- Extension direction along the first side extends, wherein at least one connected to the first collector first inlet port is provided, which extends transversely to the extension direction of the first collector, wherein the second medium via the first inlet port into the first collector can be introduced.
- the first inlet nozzle is preferably arranged tangentially to the first collector.
- the at least one first inlet pipe runs at a heat exchanger arranged as intended along the vertical or parallel to the first side or normal to the top of the heat exchanger block.
- it is also possible to provide a second inlet nozzle or a plurality of additional inlet nozzles which also extend transversely to the direction of extent, preferably parallel to the first inlet nozzle.
- the second inlet port or the additional inlet port is or are also preferably arranged tangentially to the first collector.
- the first and second sides are preferably parallel to each other and connect an underside of the heat exchanger block to a top of the
- Heat exchanger block Preferably, the top and bottom again parallel to each other, preferably the top and bottom in a
- the generally cuboid heat exchanger block of the plate heat exchanger preferably has a plurality of mutually parallel partition plates or separating plates, which form the first and second heat transfer passages.
- the outermost layers of the plate heat exchanger are covered by cover plates educated.
- the first and second heat transfer passages are preferably arranged adjacent to each other, so that the first and the second medium can exchange heat indirectly when flowing through the associated passage.
- each first heat transfer passage on the underside of the heat exchanger block has an inlet opening through which the liquid phase of the first medium can pass into the first heat transfer passages, and an outlet opening at the top of the heat exchanger block, via which the second medium at the top of the heat exchanger block as liquid or gaseous phase can escape.
- the cover plates, separator plates, fins and side bars are preferably made of aluminum and are preferably used e.g. soldered together in an oven.
- the term aluminum also includes aluminum alloys.
- the second collector along the
- Extension direction is beyond the heat exchanger block addition.
- the first pipe may be connected to the second header via a welded joint or formed integrally with the second header.
- the first pipeline via a separate, preferably annular connecting element, which is also referred to as a transition joint, connected to the second collector.
- the second header is preferably made of aluminum and the first header of a steel.
- the connecting element is preferably designed tubular and has a first end portion, which is preferably made of aluminum and with a component made of aluminum (eg second collector) is connected (eg by Welding) and a second end connected to the first end portion
- End portion made of a steel and joined to a steel member (e.g., first pipe) (e.g., by welding).
- the connecting element thus enables a connection of the different materials of the second collector and the first pipeline.
- Connecting element can over more annular material areas of the
- Connecting element to be interconnected e.g. three adjoining areas of material in the order of aluminum, titanium and nickel, wherein the connection to the aluminum end region is made via the aluminum material region and the connection to the steel-made end region is established via the nickel material region.
- the heat exchanger has a third collector arranged in the jacket space, which is in fluid communication with the at least one inlet connection, so that the second medium can flow via the third collector into the first inlet connection.
- the third collector is formed as a hollow sphere.
- the third collector is connected via a second pipe to the at least one inlet port of the first collector. If a second
- Inlet port is present (or possibly more than two inlet port), the respective further inlet port is preferably fluidly connected via a further second pipe to the third collector.
- the second pipes open in each case in the hollow spherical third collector. If only one inlet socket is present, of course, can be dispensed with the third collector.
- the third collector with a third
- Pipe is in fluid communication, which in particular goes from the third collector and through a passage opening of the shell of the shell space of the
- Heat exchanger is led out.
- the third extends
- Piping transversely to the direction of extension, preferably along the vertical or normal to the top of the heat exchanger block.
- Piping via a separate, in particular annular, connecting element is connected to the at least one inlet port (transition joint, see above).
- the second pipes are each connected via such a connecting element with the associated inlet port.
- Inlet socket made of aluminum.
- the second and / or third pipes are then preferably welded to the third collector or formed integrally therewith.
- the said connecting elements in turn then each ensure the connection between the different materials of the inlet pipe and the second pipes (see above).
- the third pipe is connected via a separate, in particular annular connecting element with the third collector.
- the third pipe is preferably made of a steel, and the third collector and the second pipes and the inlet nozzle made of aluminum.
- Pipes can then be connected to the third collector e.g. be welded or integrally formed on this. Furthermore, the second pipes can be welded to the respective inlet nozzle or integrally formed on the respective inlet nozzle.
- a direct connection is understood as meaning a connection which does not have or requires a separate connection element which is connected to the two components and is arranged between them.
- a direct connection in this sense is in particular a material connection between the relevant components (for example collector, pipeline), e.g. a welded joint.
- the two components are e.g.
- the connecting elements can be dispensed with the connecting elements according to an embodiment of the invention, when the jacket of the heat exchanger and the other Components, such as pipes, collectors, heat exchanger blocks made of aluminum or the same (in the sense above) material are made.
- the top of the heat exchanger block which is perpendicular to the two sides, to which the first and the second collector are attached and which adjoins the two sides, preferably runs at the level of the longitudinal or
- the heat exchanger according to the invention therefore advantageously has one above the top of the block
- the at least one second pipe has a curvature, so that the at least one second pipe or optionally a plurality of second pipes (see above) extends or extend in sections above the upper side of the heat transfer block along the upper side. This allows in particular the necessary flexibility for the thermal expansion of
- the second collector is mounted on the jacket of the heat exchanger, and preferably with a guide bearing, which is preferably attached to an inner side of the shell of the heat exchanger.
- the guide bearing is designed to prevent displacements of the second collector transversely to the extension means as well as heat-induced displacements in or against the latter
- Heat exchanger block of the jacket possible, for example by the second collector rests with a free end over an insulating material on the guide bearing.
- the said end of the second collector may be formed as a tubular extension of the second collector and may be closed with a flat plate so that the second medium can not escape at this end of the second header.
- the guide bearing can support the end of the second collector and
- the guide bearing may be U-shaped, wherein a bolt may be provided, which can be arranged on the guide bearing or fixable that it extends above the end of the second collector and so moving out of the end of the second collector from the
- first and / or the second collector transversely to its direction of extension have an enclosure angle
- the enclosure angle is preferably further less than 270 °, preferably less than 260 °, preferably less than 250 °, preferably less than 240 °, preferably less than 230 °, preferably less than 220 °, preferably smaller as 210 °, preferably less than 200 °.
- the enclosure angle is preferably further less than 270 °, preferably less than 260 °, preferably less than 250 °, preferably less than 240 °, preferably less than 230 °, preferably less than 220 °, preferably smaller as 210 °, preferably less than 200 °.
- Enclosing angle corresponding to the respective arcuate contour spanning center angle i.e., the angle between the two radii that run to the two ends of the circular arc contour.
- the third collector may be forged from a metal or have forged portions. So can the third
- Collector e.g. a hollow hemisphere or a hollow ball, which may be each forged.
- a heat exchanger which has only the features of the preamble of claim 1. This object can be developed by the subclaims, the preferred
- FIG. 1 is a perspective, partially sectioned view of a
- Fig. 2 is another perspective, partially sectioned view of a
- Fig. 3 is a perspective, partially sectional view of a modification of the embodiment shown in Fig. 1;
- Fig. 4 is a detail view of the guide bearing of Figure 1;
- Fig. 5 is a detail view of an alternative embodiment of the third
- FIG. 1 shows in connection with FIG. 2 a block-in-shell heat exchanger 1 according to the invention.
- the heat exchanger 1 has a jacket 3 which extends along a longitudinal or cylindrical axis L which extends along the horizontal at a heat exchanger 1 arranged as intended ,
- the jacket 3 defines a jacket space M, in which a plate heat exchanger 2 is arranged.
- This has a cuboid heat exchanger block 20, which is e.g. alternately arranged side by side and in particular vertical first and second
- Heat transfer passages 201, 202 which are each designed to receive a first and second medium S, S ', so that the two media can exchange heat indirectly.
- the heat transfer passages 201, 202 are bounded in each case by two parallel separating plates 203 (the two outermost separating plates 203 of the block 20 are referred to as cover plates), between each of which a heat conducting structure 205 is arranged, which in the present case is designed as a so-called fin, ie as a corrugated or folded sheet metal, so that together with the respective two separating plates 203 a plurality of parallel channels for the respective medium S, S 'is formed.
- the first heat transfer passages 201 are open toward the top 20c and bottom 20d (not shown).
- the second heat transfer passages 202 are additionally closed at the top and bottom by such end strips 204.
- the components of the plate heat exchanger 2 such as e.g. the partition plates 203, the fins 205, the side bars 204 and the collectors 21, 22 are preferably made of aluminum.
- the partition plates 203, side bars 204 and fins 205 are preferably soldered together in an oven. As it rises in the heat exchanger block 20, the first medium S is brought into indirect heat transfer with the second medium S ', e.g. is conducted in countercurrent in the respective adjacent second heat transfer passages 202.
- the first gaseous second medium S ' is cooled and in particular liquefied, whereas the first medium S is heated and optionally evaporated.
- a resulting gaseous phase of the first medium S accumulates in the shell space 3 above the plate heat exchanger 2 and can be deducted from there.
- first collector 21 which extends along an extension direction E over the entire first side 20 a and in Fluid communication with the individual second heat transfer passages 202 is, so that in the first collector 21 fed second medium S 'can get into the passages 202.
- at least one first inlet pipe 31 is fluid-connected to the first collector 21, the first inlet pipe 31 being arranged tangentially with respect to the first collector 21 and perpendicular to the first collector pipe 21
- Extending direction E runs, preferably along the vertical.
- the first inlet port 31 is further connected to a second pipe 42, which in turn opens into a third collector 23, which is designed hollow-spherical.
- a second (or more) inlet port 32 may be provided, which is arranged parallel to the first inlet port 31 and also opens into the first collector 21. The second inlet port 32 is then in turn
- the third collector 23 is in turn connected to a third pipe 44 in
- Heat transfer passages 202 are fed.
- the flexibility for the expansion compensation is provided completely above the top 20c of the block 20 by the second pipes 42, 43 outgoing from the respective inlet port 31, 32 are first arcuately guided over the top 20c and then open into the third collector 23.
- the top 20c of the block 20 is at the level of the central longitudinal axis L of the shell 3 and the larger shell volume compared with the volume vertically below the block 20 is located above the top 20c and allows flexible routing.
- the stubs 31, 32 or second pipes 42, 44 which pass radially from the spherical collector 23 at any position, also permit flexible cable routing, with the required wall thickness according to ASME VIII for the
- Collector / header 21 also allows a conduit with at least two bends (curved portions of the second pipes 42, 43) and as a result allows a plate heat exchanger 2, which is hardly longer along the longitudinal axis L than the block 20 with the two collectors 21, 22.
- the jacket 3 or Kettle is very compact dimensioned with small dimensions and correspondingly low refrigerant demand.
- connecting elements 52, 53 and 54 which are also referred to as transition joints.
- the connecting elements 52, 53, 54 are used for a change of material between aluminum and steel.
- Such connecting elements 52, 53 may be connected with respect to the first header 21 either between the inlet ports 31, 32 and the associated second
- Pipes 42, 43 may be arranged, in which case the inlet nozzle 31, 32 and the first collector 21 are preferably made of aluminum and the second
- Pipes 42, 43, the third collector 23 and the third pipe 44 made of steel.
- the connecting element 54 can be omitted.
- connecting elements 52 and 53 can be omitted.
- the inlet ports 31, 32, the second pipes 42, 43 and the third collector 23 are made of aluminum.
- a connecting element or transition joint 54 (see the dashed line of Figure 1) then connects the third collector 23 with the third pipe 44, which is then preferably made of steel and from the
- Mantle space M is led out (see above).
- the first collector 21 is disposed on the first side 20a of the block 2 at the edge to the top 20c.
- the second collector 22 on the second side 20b of the block 20 opposite to the first side 20a of the block 20 in the direction of the longitudinal axis L and facing away from the first side 20a, on the other hand, is disposed at the edge to the bottom 20d of the block 20 and serves for collecting and withdrawing the liquefied second medium S '.
- a first pipeline 41a aligned with the second collector 22 extends from the second collector 22 which extends along the entire second side 20b along the extension direction E and which is connected to the second collector 22 via a connecting element 51 (also referred to as transition joint, see above) connected is.
- the second collector 22 is preferably made of aluminum as the block 20, whereas the first pipe 41 a is preferably made of a steel.
- the first pipe 41 a is aligned with the second collector 22 and is through a
- the second collector 22 is hung with a free end 71 on one of the first pipe 41 a side facing away preferably in accordance with Figure 4 in a guide bearing 72 and secured there by means of a bolt 73.
- the guide bearing 72 is at a
- Extension direction E is possible. Transverse to the extension direction E, the guide bearing 72 prevents movement of the second collector 22, wherein falling out of the second collector 22 from the guide bearing 72 is prevented by the bolt 73, which together with the guide bearing 72, the free end 72 of the second collector 22nd encloses in a plane perpendicular to the direction of extension E.
- This guidance is an effective way to protect the block 20 against dynamic load cases, eg earthquakes.
- Fig. 3 shows an alternative to the figures 1 and 2 embodiment of the second
- Heat exchangers usually require multiple nozzles and manifolds, savings are possible. Thus, a manifold is completely saved and the comparatively smaller wall thickness of the spherical third collector 23 leads to material savings and reduces the weld volume. The smaller Kettle 3 also requires less coolant.
- additional drainage lines 61, 62 are provided which establish fluid communication between the third header 23 and the second header 22 and between the inlet ports 31, 32 and the second header 22.
- the drainage lines 61, 62 is shown in particular for the case that the third collector 23 is made of aluminum.
- the drainage line 61 is preferably also made of steel and is preferably connected to the first pipe 41 a, the also preferably made of steel.
- the drainage line 62 is preferably made of aluminum in each case.
- the first and the second collector 21, 22 have perpendicular to Siegreckunsgutter E preferably over an enclosure angle greater than 180 °, which causes a more favorable flow cross-section.
- the spherical third collector 23 allows several ways of nozzle orientation. Furthermore, the flow in block 20 can advantageously be controlled by the use of a plurality of inlet ports 31, 32.
- FIG. 5 finally shows an alternative embodiment of the third collector 23, which could also be used in the embodiments according to figures 1 to 3.
- the third collector 23 is designed as a hollow hemisphere, which preferably connects flush to the third pipe 44.
- the third pipe 44 may be welded to the circumference of the hemispherical third collector 23, wherein the second pipes 42, 43 as before depart from the third collector 23.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP14002262 | 2014-07-01 | ||
PCT/EP2015/001286 WO2016000812A1 (de) | 2014-07-01 | 2015-06-25 | Block-in-shell wärmeübertrager |
Publications (1)
Publication Number | Publication Date |
---|---|
EP3164656A1 true EP3164656A1 (de) | 2017-05-10 |
Family
ID=51167546
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP15731255.4A Withdrawn EP3164656A1 (de) | 2014-07-01 | 2015-06-25 | Block-in-shell wärmeübertrager |
Country Status (10)
Country | Link |
---|---|
US (1) | US20170122667A1 (de) |
EP (1) | EP3164656A1 (de) |
JP (1) | JP2017519963A (de) |
KR (1) | KR20170026583A (de) |
CN (1) | CN106471326A (de) |
AU (1) | AU2015283269A1 (de) |
CA (1) | CA2950010A1 (de) |
MX (1) | MX2016016049A (de) |
RU (1) | RU2017103104A (de) |
WO (1) | WO2016000812A1 (de) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2021093993A1 (de) | 2019-11-15 | 2021-05-20 | Linde Gmbh | Übergangsbauteil mit isolierung |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2384221A1 (fr) * | 1977-03-16 | 1978-10-13 | Air Liquide | Ensemble d'echange thermique du genre echangeur a plaques |
FI84659C (fi) * | 1989-12-14 | 1991-12-27 | Mauri Eino Olavi Kontu | Vaermevaexlare. |
FR2801341B1 (fr) * | 1999-11-22 | 2002-02-15 | Peugeot Citroen Automobiles Sa | Echangeur de chaleur pour le refroidissement de gaz d'echappement d'un vehicule automobile |
CN101977680A (zh) * | 2008-01-28 | 2011-02-16 | 弗雷穆特·J·马罗尔德 | 多列式热板和配备多列式热板的换热器 |
EP2136175B1 (de) * | 2008-06-21 | 2016-06-22 | Joachim Schult | Wärmeübertragungsplatte, Plattenpaar, Plattenpaket und Kompaktplattenwärmeüberträger sowie Verfahren zur Herstellung eines Kompaktplattenwärmeüberträgers |
EP2399668B1 (de) * | 2010-06-23 | 2014-03-12 | Freimut Joachim Marold | Verfahren zur Umsetzung insbesondere gasförmiger Reaktionsmedien |
DK2573495T3 (en) * | 2011-09-22 | 2016-09-26 | Alfa Laval Corp Ab | Thin plate evaporator of "falling film" scheme and plate evaporator device with such plate evaporator that is located in the house |
US9279417B2 (en) * | 2013-04-26 | 2016-03-08 | Sol-Electrica, Llc | Solar power system |
-
2015
- 2015-06-25 AU AU2015283269A patent/AU2015283269A1/en not_active Abandoned
- 2015-06-25 WO PCT/EP2015/001286 patent/WO2016000812A1/de active Application Filing
- 2015-06-25 US US15/316,858 patent/US20170122667A1/en not_active Abandoned
- 2015-06-25 EP EP15731255.4A patent/EP3164656A1/de not_active Withdrawn
- 2015-06-25 CN CN201580035856.5A patent/CN106471326A/zh active Pending
- 2015-06-25 KR KR1020177002908A patent/KR20170026583A/ko unknown
- 2015-06-25 MX MX2016016049A patent/MX2016016049A/es unknown
- 2015-06-25 CA CA2950010A patent/CA2950010A1/en not_active Abandoned
- 2015-06-25 RU RU2017103104A patent/RU2017103104A/ru not_active Application Discontinuation
- 2015-06-25 JP JP2016575852A patent/JP2017519963A/ja active Pending
Non-Patent Citations (2)
Title |
---|
None * |
See also references of WO2016000812A1 * |
Also Published As
Publication number | Publication date |
---|---|
AU2015283269A1 (en) | 2016-12-08 |
RU2017103104A (ru) | 2018-08-02 |
CA2950010A1 (en) | 2016-01-07 |
MX2016016049A (es) | 2017-02-23 |
WO2016000812A1 (de) | 2016-01-07 |
KR20170026583A (ko) | 2017-03-08 |
US20170122667A1 (en) | 2017-05-04 |
JP2017519963A (ja) | 2017-07-20 |
CN106471326A (zh) | 2017-03-01 |
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