EP1426565B1 - Integrierter thermische Wärmetauschergruppe für eine Dampfturbine mit organischem Fluid - Google Patents
Integrierter thermische Wärmetauschergruppe für eine Dampfturbine mit organischem Fluid Download PDFInfo
- Publication number
- EP1426565B1 EP1426565B1 EP03425722A EP03425722A EP1426565B1 EP 1426565 B1 EP1426565 B1 EP 1426565B1 EP 03425722 A EP03425722 A EP 03425722A EP 03425722 A EP03425722 A EP 03425722A EP 1426565 B1 EP1426565 B1 EP 1426565B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- condenser
- regenerator
- container
- housing
- thermal exchange
- 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.)
- Expired - Lifetime
Links
- 239000012530 fluid Substances 0.000 title claims description 16
- 239000007788 liquid Substances 0.000 claims description 11
- 238000001816 cooling Methods 0.000 claims description 5
- 230000003247 decreasing effect Effects 0.000 claims description 2
- 239000007791 liquid phase Substances 0.000 claims description 2
- 238000004519 manufacturing process Methods 0.000 claims description 2
- 230000004888 barrier function Effects 0.000 claims 1
- 239000000110 cooling liquid Substances 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002028 Biomass Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 230000001172 regenerating effect Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 238000012384 transportation and delivery Methods 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K25/00—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for
- F01K25/08—Plants or engines characterised by use of special working fluids, not otherwise provided for; Plants operating in closed cycles and not otherwise provided for using special vapours
Definitions
- This invention concerns the organic fluid steam turbine section in general and refers in particular to two thermal exchange units integrated into an organic fluid turbo generator plant (ORC)
- Such a thermal exchange group for cooling of expanded steam in a turbine is disclosed for example in document DE 100 52 414 A1 .
- the steam on exiting the turbine is obliged to pass through two thermal exchange units represented by a so-called regenerator and followed by a condenser.
- the regenerator usually requires a very large exchange surface in that the thermal exchange coefficients with a fluid in the steam phase are very low and the thermal capacity to exchange, for correct regeneration, is very high
- regenerator consequently, is bulky and its overall size is further increased by the need to realise large sized input and output steam conducts. This, at least in applications where the volumetric deliveries of the steam are very high due to the low steam pressure, typical of turbo generators for cogeneration, fed by diathermic oil heated by biomass combustion and using silicone oil as a working fluid.
- the condenser is also usually installed in a container under pressure and particular attention must be paid to the size of the input steam conducts arriving from the regenerator.
- the condenser housing must be much larger than the exchange surfaces (e.g., the tube nest in a condenser) to allow sufficient room for the steam to flow so as not to generate excessive loss in load.
- regenerator and condenser are installed in cylindrical housings suitable to resist the designed pressure, with a circular cross-section and development mainly along an axis.
- the length of the system varies from 1 to 10 times the diameter of the housing, and the diameter of the latter is normally between 0.5 and 2.5 metres, with lengths therefore in the order of 2-10 metres.
- one exchanger or regenerator 10 has a typical parallelepiped shape, with the long side parallel to the axis of a container or housing 11, for example placed horizontally so that the steam has to cross it from the top to the bottom (or from the bottom to the top).
- the objective of this invention is on the other hand to provide an innovative integration solution of the two thermal exchange units, a regenerator and a condenser for the use in the above mentioned field, really reduced in overall size, thanks to a reduction of the internal unused volumes of the container or housing they are placed in, that is those volumes which are not strictly necessary to contain the exchanger masses.
- a regenerator 21 and a condenser 22 are located in a single container or external housing 23 essentially cylindrical and on a horizontal axis and with a wall thickness suitable to contain the pressures involved.
- container 23 has, at one end, an inlet passage 24 for the hot steam coming, in the direction of arrow E, from the organic fluid steam turbine - not shown - and, at the bottom part, an exit passage 25 of the condense liquid as needed.
- the condenser 22 in which a cooling liquid circulates, is made up of a tube nest supported by a tube plate 26. According to Figs. 2-6 , the condenser is positioned at the bottom end of container 23 lying under the regenerator 21, and facing parallel to it.
- the tube plate 26 of condenser 22 has the same diameter as the container 23 and is attached to the same forming the head or bottom 23' of the part opposite to the one having the input passage 24 of the steam.
- the condenser 22 does not require a cover or container, so the exchanger group becomes particularly simple even if the tube plate 26 has to be of a specific thickness.
- the condenser 22 still maintain a partial shell, indicated by 22', which joins and integrates with the container or housing 23, extending from one head of the latter as shown in Fig.3 .
- the condenser may have a tube plate 26', with a diameter less than that of the housing and however not larger than is necessary so that it will fit on the portion of the shell 22' of the condenser.
- a tube plate smaller in diameter obviously means a significant reduction in its thickness, always however compatible with the resistance to the pressure of the design, an increase in facility of its working capacity plus less weight and a lower cost.
- the upper space 21' between the regenerator 21 and container 23 (as a cross-section, a circular sector) can house a fixed baffle 27 - Figs. 3 and 4 - as long as the regenerator itself and with a thickness less than that of the external container as the difference in pressure it has to support is little.
- This intermediate baffle 27 is shaped with the objective of forming a conveyor 28 to correctly direct the steam entering the container 23 from the turbine to the regenerator 21.
- the presence of the intermediate baffle 27, besides helping with directing the steam towards the regenerator, has the advantage of shielding and maintaining the external walls of the container colder, in that it is not directly in contact with the steam entering which is hotter. In addition it guarantees better uniformity of the temperatures of the wall of the housing, reducing in this way the possibility of warping due to dissymmetric heating.
- the flow of hot steam is forced to flow crosswise through the regenerator from the top to the bottom. Therefore any liquid which might condense on the surface of the regenerator (for example, in the start up phase when the regenerator is cold) is easily expelled by the flow of steam moving in the same direction as the force of gravity and also collects in the hot well 25.
- the liquid side of the regenerator as it is counter current, is traversed from bottom to top so any incondensable air or other gas is pushed away, giving the natural rise (from bottom to top) inside the mass of liquid the right of way.
- the condenser 22 underneath is fed almost in a uniform fashion for all its length.
- the lower part of the container is used to house the tube nest of the condenser, completely without the need for its own cover as in Fig. 2 , or for most of it as in Fig.3 , where the condenser maintains a portion of the shell 22' which may be shaped so as to collect and expel any incondensable gasses which may get into the circuit.
- Another improvement in the thermal exchange conditions to the condenser can be achieved by equipping the latter, at least in the lower section, with side walls 29 as shown in Fig. 5 .
- These walls have the aim of compelling the steam to pass inside the tube nest flowing mainly from top to bottom. This favours the downward collection of the liquid resulting from condensation and the downward discharge of any incondensable gas present.
- the incondensable gas accumulated at the bottom gradually moves towards the tube plate from where it will be extracted.
- containing and guide side walls 29 for downward steam flow enables the flow of the cooling liquid, water or other vehicle, to come into contact with the different parts of the condensing tube nest in an orderly fashion compared with the steam flow.
- regenerator 21 and condenser 22 are housed in a common container or housing 23, but this container is provided with walls 30 which set the passage of the steam, compelling it to cross first the regenerator and then the condenser in a fundamentally horizontal direction.
- regenerator 21 and condenser 22 are housed in a common container or housing 23. But the condenser 22 is placed above the regenerator 21 with an opportune collection and discharge system 31 of the condense liquid placed between the two exchangers 21, 22.
- the condense liquid is in this way at a higher level from the ground than from the cases of realisations where the condenser is placed below the regenerator.
- NPSHa suction height available to the pump
- the liquid which forms collects at the bottom of the housing and can be removed either by evaporation, thanks to a heater coil 32, or by means of an auxiliary pump 33. Also in this case a baffle 34 can be placed in the bottom internal part of the housing 23 so as to direct the steam from the entry E towards the regenerator.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Claims (9)
- Wärmetauschgruppe zur Abkühlung eines ausgedehnten Dampfes in einer Turbine zur Erzeugung elektrischer Energie die als verdampfbares Arbeitsfluid ein organisches Fluid mit hohem Molekulargewicht benutzt, wobei die genannte Gruppe einen Wiederhersteller (21) zum Vorwärmen des Arbeitsfluids in einer flüssigen Phase mittels heißem Dampf der aus einer Turbine austretet und einen Kondensator (22) zum Abkühlen des Gases bis zu einer Verdichtungstemperatur umfasst, wobei der genannte Wiederhersteller und der genannte Kondensator in einem einzigen Behälter oder äußeren Gehäuse (23) mit einer Eingangsleitung (24) für den heißen Dampf und mit einem Ausgangsdurchlass (25) für die verdichtete Flüssigkeit gestellt sind und wobei der Behälter oder das Gehäuse (23) im wesentlichen zylindrisch um einer waagerechten Achse zum Eingang des heißen Dampfes und zum Ausgang der flüssigen Verdichtung sind, dadurch gekennzeichnet dass der genannte Dampfeingang stirn- oder endseitig am Gehäuse steht und der genannte Verdichtungsausgang in einem Grundabschnitt des genannten Behälters oder äußeren Gehäuses steht und dass der Wiederhersteller länglich und quer an einer mittleren Höhe des Behälters oder des äußeren Gehäuses (23) verläuft, und dass der Kondensator unterhalb oder oberhalb und parallel zum Wiederhersteller stirn- oder endseitig vom Behälter oder Gehäuse ablaufend gegenüberliegend zu dem mit der Eingangsleitung für den heißen Dampf liegt und dass der Wiederhersteller mit einem Abschnitt des genannten Behälters oder Gehäuses einen Raum (21') zur Verteilung des heißen Dampfes zum Wiederhersteller und dem Kondensator hin umgrenzt.
- Wärmetauschgruppe nach Anspruch 1, wobei im Raum zwischen dem Wiederhersteller (21) und dem genannten Abschnitt des Behälters oder des äußeren Gehäuses (23) einen fixierten Stromstörer (27, 34) liegt, der einen Förderer (28) bildet der den eingehenden heißen Dampf zu den Wiederhersteller hin leitet und der eine den genannten Kopfabschnitt des Behälters oder des Gehäuses schützende Sperre bildet.
- Wärmetauschgruppe nach Anspruch 2, wobei der genannte Stromstörer für die gesamte Länge des Wiederherstellers verläuft und wobei dieser eine Leitung definiert, die einen vom Eingang des heißen Dampfes abgehend schrittweise abnehmenden Querschnitt hat.
- Wärmetauschgruppe nach einem der vorhergehenden Anspruche, wobei der Kondensator auf entgegengesetzte Seiten mit zwei Seitenwänden (29) versehen ist, die den Dampf zwingen durch den Kondensator zu fließen, wobei die genannten Seitenwände in Kontakt mit zumindest einem unteren Teil des Kondensators sind.
- Wärmetauschgruppe nach einem der vorhergehenden Anspruche, wobei der Kondensator (22) aus zumindest einem von einer Rohrplatte (26) gestützten Rohrsatz zusammengebaut ist und wobei die genannte Rohrplatte mit dem Behälter oder mit dem äußeren Gehäuse (23) angeschlossen ist um die Stirn oder das Ende des genannten Gehäuses auf der gegenüberliegenden Seite zu der in der die Eingangsleitung des heißen Dampfes unterbracht ist zu bilden.
- Wärmetauschgruppe nach einem der vorhergehenden Ansprüche, wobei in dem Behälter oder in dem äußeren Gehäuse, zwischen dem Wiederhersteller und dem Kondensator, Wände vorhergesehen sind, die den Dampf dazu zwingen durch den Wiederhersteller in im Wesentlich horizontaler Richtung zu fließen.
- Wärmetauschgruppe nach einem der vorhergehenden Ansprüche, wobei der Widerhersteller und der Kondensator keine eigene Deckung haben, haben aber den Behälter oder das äußere Gehäuse gemeinsam als Gerüst.
- Wärmetauschgruppe nach einem der Anspruche von 1 bis 6, wobei der Kondensator einen Gerüstabschnitt (22') besitzt der in Kontakt mit der Stirn oder mit dem Ende des Behälters oder des äußeren Gehäuses liegt und sich mit diesen integriert, von der gegenüberliegenden Seite zu der in der die Eingangsleitung des heißen Dampfes unterbracht ist.
- Wärmetauschgruppe nach Anspruch 8, wobei der Kondensator aus zumindest einem von einer Rohrplatte (26') gestützten Rohrsatz zusammengebaut ist, der mit dem Gerüstabschnitt (22') angeschlossen ist, wobei der genannte Rohrsatz einen Durchschnitt hat der kleiner als den des Behälters oder des äußeren Gehäuse (21) ist.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ITBS20020102 ITBS20020102A1 (it) | 2002-11-11 | 2002-11-11 | Gruppo di scambio termico integrato per turbine a vapore di fluido |
ITBS20020102 | 2002-11-11 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1426565A1 EP1426565A1 (de) | 2004-06-09 |
EP1426565B1 true EP1426565B1 (de) | 2013-03-27 |
Family
ID=32310133
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP03425722A Expired - Lifetime EP1426565B1 (de) | 2002-11-11 | 2003-11-06 | Integrierter thermische Wärmetauschergruppe für eine Dampfturbine mit organischem Fluid |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP1426565B1 (de) |
IT (1) | ITBS20020102A1 (de) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2024084359A1 (en) * | 2022-10-19 | 2024-04-25 | Turboden S.p.A. | Recuperator with external manifolds for organic rankine cycle plants |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102008038241A1 (de) | 2008-08-18 | 2010-02-25 | Eckert, Frank | Wärmetauschersystem für Rankine-Prozesse |
DE202008010988U1 (de) | 2008-08-18 | 2008-12-24 | Eckert, Frank | Wärmetauschersystem für Rankine-Prozesse |
WO2013150018A2 (en) | 2012-04-03 | 2013-10-10 | Equitherm S.À R.L. | Device for power generation according to a rankine cycle |
CN208332761U (zh) | 2018-01-16 | 2019-01-04 | 开利公司 | 用于冷凝器的导流板、具有其的冷凝器及制冷系统 |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4067189A (en) * | 1974-12-16 | 1978-01-10 | The Hydragon Corporation | Multicycle turbine engine |
US4185465A (en) * | 1976-01-29 | 1980-01-29 | Dunham-Bush, Inc. | Multi-step regenerated organic fluid helical screw expander hermetic induction generator system |
DE19907512A1 (de) * | 1999-02-22 | 2000-08-31 | Frank Eckert | Vorrichtung zur Energieumwandlung auf der Basis von thermischen ORC-Kreisprozessen |
DE10052414A1 (de) * | 2000-10-23 | 2002-05-08 | Frank Eckert | Verfahren zum Betreiben einer Energieumwandlungseinrichtung sowie Vorrichtung zur Durchführung eines solchen Verfahrens |
-
2002
- 2002-11-11 IT ITBS20020102 patent/ITBS20020102A1/it unknown
-
2003
- 2003-11-06 EP EP03425722A patent/EP1426565B1/de not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2024084359A1 (en) * | 2022-10-19 | 2024-04-25 | Turboden S.p.A. | Recuperator with external manifolds for organic rankine cycle plants |
Also Published As
Publication number | Publication date |
---|---|
ITBS20020102A1 (it) | 2004-05-12 |
EP1426565A1 (de) | 2004-06-09 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4621681A (en) | Waste heat boiler | |
EP2278145B1 (de) | Kogenerationsvorrichtung | |
US4482004A (en) | Waste heat boiler | |
CN110006019B (zh) | 一种悬空结构蒸汽发生器 | |
EP0027055A1 (de) | Heizkessel | |
US8069906B2 (en) | Vehicular exhaust heat recovery apparatus with frozen working fluid melting | |
EP1426565B1 (de) | Integrierter thermische Wärmetauschergruppe für eine Dampfturbine mit organischem Fluid | |
RU2403522C2 (ru) | Способ нагрева и/или испарения органической среды и теплообменный блок для извлечения теплоты от потока горячего газа | |
EP1096128B1 (de) | Rückgewinnungsvorrichtung für die Abwärme einer Brennkraftmaschine | |
EP0441315B1 (de) | Heizgerät mit grossem Wirkungsgrad | |
FI90313C (fi) | Välinestekuumennin levymäisiä kalvohaihduttimia varten ja menetelmä nesteen haihduttamiseksi | |
CN109539839B (zh) | 一种智能控制的环路热管换热器 | |
GB2149484A (en) | Condensation boiler | |
CN216897625U (zh) | 空调式油烟机及其空调模块 | |
US20070028864A1 (en) | Heating arrangement | |
WO2013190367A2 (en) | Heat exchange means for cooking devices and methods for retrofitting cooking devices | |
US5791158A (en) | Internally fired generator with improved solution flow | |
CN114264003A (zh) | 空调式油烟机、空调模块及其控制方法 | |
RU62688U1 (ru) | Секция предварительного подогрева воздуха | |
CN109539845B (zh) | 一种双温度智能协调控制的换热器 | |
CN104633938B (zh) | 电锅炉换热器 | |
KR20010107891A (ko) | 가정용 보일러 | |
EP4209720A1 (de) | Hybrider kessel | |
CN216953545U (zh) | 燃气热水设备 | |
CN216952990U (zh) | 低压高温蒸汽模块 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LI LU MC NL PT RO SE SI SK TR |
|
AX | Request for extension of the european patent |
Extension state: AL LT LV MK |
|
17P | Request for examination filed |
Effective date: 20041203 |
|
AKX | Designation fees paid |
Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LI LU MC NL PT RO SE SI SK TR |
|
17Q | First examination report despatched |
Effective date: 20060925 |
|
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: TURBODEN S.R.L. |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IT LI LU MC NL PT RO SE SI SK TR |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: EP |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: REF Ref document number: 603544 Country of ref document: AT Kind code of ref document: T Effective date: 20130415 |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R096 Ref document number: 60343605 Country of ref document: DE Effective date: 20130523 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BG Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130627 Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130327 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130327 Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130628 Ref country code: SI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130327 |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: VDEP Effective date: 20130327 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130327 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130327 Ref country code: EE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130327 Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130729 Ref country code: RO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130327 Ref country code: CZ Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130327 Ref country code: SK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130327 Ref country code: ES Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130708 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: CY Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130327 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130327 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed |
Effective date: 20140103 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R097 Ref document number: 60343605 Country of ref document: DE Effective date: 20140103 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20131106 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20131130 Ref country code: MC Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130327 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20131130 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST Effective date: 20140731 |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: MM4A |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20131106 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20131106 Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20131202 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: HU Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO Effective date: 20031106 Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20131106 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: TR Payment date: 20211103 Year of fee payment: 19 Ref country code: AT Payment date: 20211027 Year of fee payment: 19 Ref country code: DE Payment date: 20211013 Year of fee payment: 19 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: IT Payment date: 20221118 Year of fee payment: 20 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R119 Ref document number: 60343605 Country of ref document: DE |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: MM01 Ref document number: 603544 Country of ref document: AT Kind code of ref document: T Effective date: 20221106 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: AT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20221106 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20230601 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: TR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20221106 |