EP1116862A2 - Procédé et installation de production de vapeur - Google Patents

Procédé et installation de production de vapeur Download PDF

Info

Publication number
EP1116862A2
EP1116862A2 EP00126349A EP00126349A EP1116862A2 EP 1116862 A2 EP1116862 A2 EP 1116862A2 EP 00126349 A EP00126349 A EP 00126349A EP 00126349 A EP00126349 A EP 00126349A EP 1116862 A2 EP1116862 A2 EP 1116862A2
Authority
EP
European Patent Office
Prior art keywords
steam generator
feed water
waste heat
steam
heat boiler
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
Application number
EP00126349A
Other languages
German (de)
English (en)
Other versions
EP1116862B1 (fr
EP1116862A3 (fr
Inventor
Bernd Gericke
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
MAN Energy Solutions SE
Original Assignee
MAN Turbomaschinen AG GHH Borsig
MAN Turbomaschinen AG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by MAN Turbomaschinen AG GHH Borsig, MAN Turbomaschinen AG filed Critical MAN Turbomaschinen AG GHH Borsig
Publication of EP1116862A2 publication Critical patent/EP1116862A2/fr
Publication of EP1116862A3 publication Critical patent/EP1116862A3/fr
Application granted granted Critical
Publication of EP1116862B1 publication Critical patent/EP1116862B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22—STEAM GENERATION
    • F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B1/00—Methods of steam generation characterised by form of heating method
    • F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
    • F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
    • F22B1/183—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines in combination with metallurgical converter installations
    • 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
    • F01K3/00—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein
    • F01K3/18—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein having heaters
    • F01K3/185—Plants characterised by the use of steam or heat accumulators, or intermediate steam heaters, therein having heaters using waste heat from outside the plant

Definitions

  • the invention relates to a method for generating steam in a steam generator system with a gas fired with blast furnace gas Steam generator and a steam generator system.
  • the invention is based on the object of the generic type Developing processes in such a way that they are based on support firing with noble fuels in the combustion of the blast furnace gas in Continuous operation can be dispensed with.
  • Waste heat is generated in sinter cooling systems in metallurgical plants, in which at the same time top gas as waste gas from the blast furnace process is produced. From the sintered fine ores to the cooling air emitted heat is over according to the invention Heat exchanger surfaces in the waste heat boiler by Heat transfer system in the high pressure system of the steam generator coupled. So that waste heat with different and especially low temperature level and waste gas with fluctuating and in particular low calorific value for generation exploited by steam.
  • the heat utilization in the area of the sinter cooling systems is designed due to the special temperature and Cooling air quantity ratios are particularly complex.
  • Cooling air is extracted from heat, making heat sources different Temperature levels arise.
  • a special waste heat boiler concept is required.
  • the most interesting part of the waste heat from the Sinter cooling system only makes up a small percentage of the total amount of cooling air. While this is proportionate low cooling air mass flow thanks to its higher gas temperature lends itself particularly to high feed water preheating the larger cooling air mass flow with low temperature remaining feed water preheating used.
  • the temperature of the feed water is checked before entering the Heat exchanger surfaces of the waste heat boiler on the physical lowest possible value lowered. It is advantageous if the feed water through the heat exchange with the recycled steam turbine condensate is cooled. The on this way, lowered temperature of the feed water also allows extract heat from the low-temperature sintered cooling air.
  • the heat transfer system consists of two external ones additional preheaters, some of which is the waste heat Add top gas to all combustion air and fuel. This increases the calorific value of the blast furnace gas to such an extent that in normal operation no support fire over high calorific Noble fuels like natural gas is necessary.
  • FIG. 1 An embodiment of the invention is in the drawing shown and is explained in more detail below.
  • the drawing shows a process scheme for generating steam.
  • a steam generator 1 which works according to the natural circulation principle contains a combustion chamber 2, the one from top to bottom flowed flue gas duct 3 is connected. By doing Flue gas duct 3 are secondary heating surfaces like superheater 4 and the convection evaporator 4a. Instead of one Maturum steam generator can also be a forced circulation or a Forced-flow steam generators are used. It can also another than the flue gas duct shown, e.g. B. according to Art a tower boiler can be used.
  • the steam generator 1 is fired with blast furnace gas.
  • the combustion chamber 2 is shown on the front side with only schematically Provide burners 5.
  • the burners 5 have an air line 6 for supplying combustion air and with a top gas line 7 connected to the supply of blast furnace gas.
  • This emergency fuel is fed to the burners 5 via a gas line 8.
  • a steam line 9 is connected to the superheater 4 of the steam generator 1 connected, which is guided to a steam turbine 10.
  • the Steam turbine 10 has a generator 11 for generating electricity coupled.
  • the steam turbine 10 can be regulated Withdrawal 12 process steam can be extracted into a steam network is fed.
  • the outlet of the steam turbine 10 is connected to an exhaust steam line 13 connected, which is led to a capacitor 14.
  • Condenser 14 the exhaust steam is condensed, and that Steam turbine condensate is in via a condensate line 15 a feed pump 16 is arranged to a degasser 17 promoted.
  • the degasser 17 is operated with bleed steam is removed from the steam turbine 10 via a bleed line 18.
  • a feed water line 19 is connected to the degasser 17 connected in which a feed water pump 20 is arranged, which the pressure of the feed water to the process pressure of the Steam generator 1 increased.
  • the feed water line 19 is between the degasser 17 and the feed water pump 20 Water / water heat exchanger 21 arranged, the at the same time the condensate line 15 is connected.
  • the feed water line 19 is connected in parallel Heat exchanger surfaces 22 performed in a waste heat boiler 23rd are arranged. Downstream from the heat exchanger surfaces 22 is the feed water line 19 with an external air preheater 24, to which the air line 6 is connected, and in parallel for this purpose with a gas preheater 25 to which the top gas line 7 connected, connected. Following the air preheater 24 and the gas preheater 25 is the feed water line 19 a feed water preheater 26 led by the flue gas is flowed through, which leaves the steam generator 1. This Feed water preheater 26 is on the water side with the water-steam cycle of the steam generator 1 connected.
  • the waste heat boiler 23 is a sintering system for sintering Subsequent fine ores on a sintered belt.
  • the Sintering process becomes air that rests on the sintering belt Layer of the sintered mixture or the sinter supplied. Through the Air becomes the sintering process through the combustion of the Maintain sintered mixture of mixed fine coal.
  • To Sintering is carried out by additional fans with cooling air pressed or sucked the sinter. This way it falls lengthways of the sintered cooling belt SK1 in the gas flue 30 with exhaust air different temperatures and in different amounts or, as shown in the throttle cable 31, cooling air with a corresponding mixing temperature on the sintered cooling belt SK2.
  • the waste heat boiler 23 is divided into two and has two throttle cables 30, 31.
  • the heat exchanger surfaces 22 are distributed to these two throttle cables 30, 31.
  • the throttle cables 30, 31 des Waste heat boilers 23 are with connecting pieces for the different exhaust gas flows 27, 28, 29 provided.
  • Both sinter cooling systems SK1 and SK2 can be used to the heat extraction described above also in series be switched.
  • the feed water is before entering the Heat exchanger surfaces 22 of the waste heat boiler 23 on the physically lowest possible temperature cooled. Consists due to the composition of the waste heat boiler 23 exhaust gases flowing through there is no risk that a Below the dew point, the corrosion damage to the Heat exchanger surfaces causes, as described, that Feed water through before entering the heat exchanger surfaces Steam turbine condensate cooled. This usually happens Waste heat boilers in which exhaust air from sintered cooling belts is cooled becomes. However, corrosion damage must be expected, so the temperature of the feed water must be before entering the Heat exchanger surfaces 22 of the waste heat boiler 23 approximately Temperature of the degasser 17 correspond.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Sustainable Development (AREA)
  • Sustainable Energy (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Thermal Sciences (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Air Supply (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Degasification And Air Bubble Elimination (AREA)
  • Physical Water Treatments (AREA)
EP00126349A 2000-01-15 2000-12-02 Procédé et installation de production de vapeur Expired - Lifetime EP1116862B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10001512 2000-01-15
DE10001512A DE10001512A1 (de) 2000-01-15 2000-01-15 Verfahren zur Erzeugung von Dampf und eine Dampferzeugeranlage

Publications (3)

Publication Number Publication Date
EP1116862A2 true EP1116862A2 (fr) 2001-07-18
EP1116862A3 EP1116862A3 (fr) 2002-09-25
EP1116862B1 EP1116862B1 (fr) 2005-02-09

Family

ID=7627638

Family Applications (1)

Application Number Title Priority Date Filing Date
EP00126349A Expired - Lifetime EP1116862B1 (fr) 2000-01-15 2000-12-02 Procédé et installation de production de vapeur

Country Status (4)

Country Link
EP (1) EP1116862B1 (fr)
AT (1) ATE288997T1 (fr)
DE (2) DE10001512A1 (fr)
ES (1) ES2235747T3 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9604864B2 (en) 2013-03-12 2017-03-28 Ingenica Ingenierie Industrielle Steam generation method and method for recovering crude oil by steam-assisted gravity drainage (SAGD) including said steam generation method
US10054308B2 (en) 2014-09-11 2018-08-21 Ingenica Ingenierie Industrielle Method for generating steam from raw water, in particular from blow down water coming from a steam generator

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101294502B (zh) * 2007-04-23 2010-12-08 张庆玉 多功能真空火力水力双发电和提水调水站

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4327476A1 (de) * 1993-08-16 1995-02-23 Steinmueller Gmbh L & C Verfahren zum Betrieb eines mit fossilen Brennstoffen befeuerten Dampferzeugers und Dampferzeugungsanlage zur Durchführung des Verfahrens
DE29608816U1 (de) * 1996-05-15 1996-08-01 Deutsche Babcock Babcock Lentjes Kraftwerkstechnik GmbH Standort Berlin, 10407 Berlin Anordnung zur Nutzung der Abwärme von Zementklinkerlinien
DE19645322A1 (de) * 1996-11-04 1998-05-07 Asea Brown Boveri Kombinierte Kraftwerksanlage mit einem Zwangsdurchlaufdampferzeuger als Gasturbinen-Kühlluftkühler
JPH11325406A (ja) * 1998-05-07 1999-11-26 Ebara Corp 火力発電設備における給水加熱装置

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2243380C3 (de) * 1972-09-04 1978-07-20 Kraftwerk Union Ag, 4330 Muelheim Dampfkraftanlage mit rauchgasbeheiztem Speisewasservorwärmer und wasserbeheiztem Luftvorwärmer
DE3324283A1 (de) * 1983-07-06 1985-01-24 Kleinewefers Energie- und Umwelttechnik GmbH, 4150 Krefeld Sinterbandanlage mit einrichtung fuer die abhitzeverwertung

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4327476A1 (de) * 1993-08-16 1995-02-23 Steinmueller Gmbh L & C Verfahren zum Betrieb eines mit fossilen Brennstoffen befeuerten Dampferzeugers und Dampferzeugungsanlage zur Durchführung des Verfahrens
DE29608816U1 (de) * 1996-05-15 1996-08-01 Deutsche Babcock Babcock Lentjes Kraftwerkstechnik GmbH Standort Berlin, 10407 Berlin Anordnung zur Nutzung der Abwärme von Zementklinkerlinien
DE19645322A1 (de) * 1996-11-04 1998-05-07 Asea Brown Boveri Kombinierte Kraftwerksanlage mit einem Zwangsdurchlaufdampferzeuger als Gasturbinen-Kühlluftkühler
JPH11325406A (ja) * 1998-05-07 1999-11-26 Ebara Corp 火力発電設備における給水加熱装置

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
PATENT ABSTRACTS OF JAPAN vol. 2000, no. 02, 29. Februar 2000 (2000-02-29) & JP 11 325406 A (EBARA CORP), 26. November 1999 (1999-11-26) *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9604864B2 (en) 2013-03-12 2017-03-28 Ingenica Ingenierie Industrielle Steam generation method and method for recovering crude oil by steam-assisted gravity drainage (SAGD) including said steam generation method
US10054308B2 (en) 2014-09-11 2018-08-21 Ingenica Ingenierie Industrielle Method for generating steam from raw water, in particular from blow down water coming from a steam generator

Also Published As

Publication number Publication date
EP1116862B1 (fr) 2005-02-09
EP1116862A3 (fr) 2002-09-25
DE50009474D1 (de) 2005-03-17
DE10001512A1 (de) 2001-07-19
ATE288997T1 (de) 2005-02-15
ES2235747T3 (es) 2005-07-16

Similar Documents

Publication Publication Date Title
DE69102577T2 (de) Kraftanlage.
DE3240373A1 (de) Verfahren und vorrichtung zur rauchgasentschwefelung von kohlenfeuerungen
EP0191141B1 (fr) Procédé et installation pour la réduction de la teneur en NOx dans le gaz brûlé lors de la combustion de combustibles fossiles dans des installations de chauffage
EP2167794B1 (fr) Dispositif et procédé de production de force et de chaleur
WO2009100881A4 (fr) Centrale au charbon et procédé d'exploitation de la centrale au charbon
DE2831027C2 (de) Verfahren und Vorrichtung zur Flugstromvergasung
EP0648323B1 (fr) Centrale thermique a vapeur permettant de produire de l'energie electrique
EP0122534B1 (fr) Procédé pour le fonctionnement d'une installation de craquage d'hydrocarbures
DE4323469C2 (de) Verfahren zum Betrieb eines mit einem trocknungsbedürftigen Brennstoff, insbesondere mit Braunkohle, befeuerten Kraftwerks
DE3204672A1 (de) Kombinierter gas-/dampfturbinenprozess
EP1099042A2 (fr) Installation a turbine a gaz et a vapeur
DE3225140C2 (fr)
EP1116862B1 (fr) Procédé et installation de production de vapeur
EP0267206B1 (fr) Procede et installation de reduction des emissions d'oxyde nitrique lors de la combustion de houille a haute et a moyenne teneur en matieres volatiles
DE19734862C2 (de) Wärmekraftwerk mit einer Gasturbine und einem Dampferzeuger für eine Mehrdruck-Dampfturbine
DE3617364A1 (de) Kombiniertes gas- und dampfturbinenkraftwerk mit aufgeladener wirbelschichtfeuerung und kohlevergasung
DE4418342C2 (de) Verfahren zum Betrieb eines mit einem trocknungsbedürftigen Brennstoff befeuerten Kraftwerkes
DE3111674A1 (de) "verfahren zur herstellung von kohlenstaub als brennstoff fuer kohlenstaub-zuendbrenner"
DE4327476C2 (de) Verfahren zum Betrieb eines mit fossilen Brennstoffen gefeuerten Dampferzeugers und Dampferzeugungsanlage
EP0618404B1 (fr) Procédé et installation pour la génération de vapeur dans une centrale de puissance et de chaleur
DE2533169A1 (de) Anlage zur herstellung von zement im trockenverfahren
DE3842325C2 (de) Mehrzug-Abhitzekessel mit Zusatzfeuerung
DE112010005234T5 (de) Energierückgewinnung aus Gasen in einer Hochofenanlage
DE3009237A1 (de) Verfahren zur strom- und waermeerzeugung aus kohle
DE4220489C1 (en) Operating air heater plant - using boiler heated closed circuit to preheat air and fuel feeds to reducing high value combustion fuels

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: A2

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR

AX Request for extension of the european patent

Free format text: AL;LT;LV;MK;RO;SI

PUAL Search report despatched

Free format text: ORIGINAL CODE: 0009013

AK Designated contracting states

Kind code of ref document: A3

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR

AX Request for extension of the european patent

Free format text: AL;LT;LV;MK;RO;SI

RAP1 Party data changed (applicant data changed or rights of an application transferred)

Owner name: MAN TURBOMASCHINEN AG

17P Request for examination filed

Effective date: 20020910

RAP1 Party data changed (applicant data changed or rights of an application transferred)

Owner name: MAN TURBOMASCHINEN AG

AKX Designation fees paid

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR

GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

RAP1 Party data changed (applicant data changed or rights of an application transferred)

Owner name: MAN TURBO AG

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR

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 FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20050209

Ref country code: IE

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: 20050209

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: 20050209

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: 20050209

REG Reference to a national code

Ref country code: GB

Ref legal event code: FG4D

Free format text: NOT ENGLISH

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

Free format text: GERMAN

REF Corresponds to:

Ref document number: 50009474

Country of ref document: DE

Date of ref document: 20050317

Kind code of ref document: P

GBT Gb: translation of ep patent filed (gb section 77(6)(a)/1977)

Effective date: 20050318

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

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: 20050509

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: 20050509

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: 20050509

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2235747

Country of ref document: ES

Kind code of ref document: T3

NLV1 Nl: lapsed or annulled due to failure to fulfill the requirements of art. 29p and 29m of the patents act
REG Reference to a national code

Ref country code: IE

Ref legal event code: FD4D

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: 20051202

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

ET Fr: translation filed
PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LU

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20051231

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20051231

Ref country code: MC

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20051231

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20051231

26N No opposition filed

Effective date: 20051110

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: PT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20050709

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: ES

Payment date: 20081217

Year of fee payment: 9

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20090130

Year of fee payment: 9

BERE Be: lapsed

Owner name: *MAN TURBO A.G.

Effective date: 20091231

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 NON-PAYMENT OF DUE FEES

Effective date: 20091231

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 20110329

REG Reference to a national code

Ref country code: DE

Ref legal event code: R081

Ref document number: 50009474

Country of ref document: DE

Owner name: MAN DIESEL & TURBO SE, DE

Free format text: FORMER OWNER: MAN TURBO AG, 46145 OBERHAUSEN, DE

Effective date: 20110325

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: ES

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20110316

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: ES

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20091203

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 16

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20151210

Year of fee payment: 16

Ref country code: GB

Payment date: 20151221

Year of fee payment: 16

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20151221

Year of fee payment: 16

Ref country code: AT

Payment date: 20151222

Year of fee payment: 16

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: IT

Payment date: 20151228

Year of fee payment: 16

REG Reference to a national code

Ref country code: DE

Ref legal event code: R119

Ref document number: 50009474

Country of ref document: DE

REG Reference to a national code

Ref country code: AT

Ref legal event code: MM01

Ref document number: 288997

Country of ref document: AT

Kind code of ref document: T

Effective date: 20161202

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20161202

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

Effective date: 20170831

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: 20161202

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20170102

Ref country code: IT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20161202

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: 20170701

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20161202