[go: up one dir, main page]

EP1046861B1 - Procédé pour le réglage automatique de la combustion d'un incinerateur d'ordures - Google Patents

Procédé pour le réglage automatique de la combustion d'un incinerateur d'ordures Download PDF

Info

Publication number
EP1046861B1
EP1046861B1 EP00105630A EP00105630A EP1046861B1 EP 1046861 B1 EP1046861 B1 EP 1046861B1 EP 00105630 A EP00105630 A EP 00105630A EP 00105630 A EP00105630 A EP 00105630A EP 1046861 B1 EP1046861 B1 EP 1046861B1
Authority
EP
European Patent Office
Prior art keywords
flue gas
refuse
waste
mass flow
oil
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
Application number
EP00105630A
Other languages
German (de)
English (en)
Other versions
EP1046861A1 (fr
Inventor
Peter Dübendorfer
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.)
Martin GmbH fuer Umwelt und Energietechnik
Original Assignee
Martin GmbH fuer Umwelt und Energietechnik
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 Martin GmbH fuer Umwelt und Energietechnik filed Critical Martin GmbH fuer Umwelt und Energietechnik
Publication of EP1046861A1 publication Critical patent/EP1046861A1/fr
Application granted granted Critical
Publication of EP1046861B1 publication Critical patent/EP1046861B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/50—Control or safety arrangements
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2207/00—Control
    • F23G2207/10—Arrangement of sensing devices
    • F23G2207/104—Arrangement of sensing devices for CO or CO2
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2207/00—Control
    • F23G2207/20—Waste supply
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2900/00—Special features of, or arrangements for incinerators
    • F23G2900/55—Controlling; Monitoring or measuring
    • F23G2900/55003—Sensing for exhaust gas properties, e.g. O2 content
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2900/00—Special features of, or arrangements for incinerators
    • F23G2900/55—Controlling; Monitoring or measuring
    • F23G2900/55011—Detecting the properties of waste to be incinerated, e.g. heating value, density

Definitions

  • the invention is a method for automatic adjustment the firing of a waste incineration plant.
  • a method for optimized driving of a waste incineration plant which regulates the amount of air in dependence on the calorific value.
  • the combustion air can be adjusted in individual zones. This is done continuously to adjust the amount to a fluctuating calorific value.
  • the calorific value results from the quotient of currently released heat and the waste mass flow.
  • the CO and the O 2 content of the exhaust gas are included.
  • the water content of the waste is not considered disadvantageous in this process, although it plays a major role in combustion.
  • the invention overcomes the mentioned disadvantages. It solves the task To provide a method for determining the quality of waste, which is simple and works reliably. If a flue gas scrubber is present, the process should only temperature, pressure and differential measurements (eg volume flow) apply. It should also be easy in an existing waste incineration plant can be integrated and be cost effective.
  • this is achieved by setting a fictitious process variable "waste quality" from the calorific value of the refuse (Hu) and the water content of the refuse (H 2 ) in order to adjust the firing variables, such as combustion air distribution, waste layer thickness and rust velocity O garbage ) is determined.
  • a flue gas scrubber is by the inventive method the direct measurement of the water content superfluous.
  • Next can be beneficial over a statistical relationship between the heat of combustion and the Carbon mass flow determined by the combustion of water become.
  • the process is simple and inexpensive in an existing Waste incineration plant can be integrated, since usually all necessary equipment already available. Despite the simplicity, it is a very reliable procedure.
  • the inventive method is suitable by determining the values of water content of the waste H 2 O garbage and Calorific value of garbage Hu In a waste incineration plant to set a fictitious size "waste quality" and thereby make an automatic firing adjustment, for example, in relation to major variables such as the combustion air distribution, the waste layer thickness or the rust rate.
  • FIGS. 3 and 4 schematically show the first method step in a waste incineration plant 10 with a furnace 40.
  • This type of waste throughput calculation further requires that more or less always be loaded at the same mark 30 in the refuse chute 50 (eg, a weld, the deflection edge or the field of view of the camera). This means that the volume decrease between 2 feeds corresponds to a gripper content.
  • the boiler efficiency, En boiler , the enthalpy of feed water h SPW and live steam h FD and the live steam quantity m ⁇ FD of the garbage heating value Hu can be calculated.
  • the flue gas moisture serves as a basis for the determination of the water content in the Rubbish.
  • the water content in the garbage can not directly due to lack of suitable measuring systems be detected.
  • the flue gas moisture must increase. This process is shown in FIG.
  • the flue gas moisture H 2 O flue gas can be calculated with an existing scrubber from the flue gas temperature before scrubber and the saturation temperature in the scrubber.
  • the drier the flue gas the more water it can absorb and the lower the saturation temperature in the scrubber. If no scrubber is present, the flue gas moisture H 2 O flue gas is determined directly, for example, with a measurement based on laser absorption (at the corresponding frequency).
  • m H 2 O _ flue gas V Rauchgas_Kesselende ⁇ H 2 O flue gas ⁇ ⁇ H2O_Dampf
  • H 2 O_Verbrennungs Kunststoff ( V PL + V SL + V secondary air ) ⁇ H 2 O combustion air
  • H 2 O combustion air is between 7..12g / Nm 3 and is assumed to be constant in this range.
  • Figure 9 is a diagram showing some examples of how an error of garbage mass flow m ⁇ garbage, NCV and water mass flow m ⁇ H2O_müll changes in relation to the waste quality.
  • Waste quality f (Hu rubbish . H 2 O rubbish ) can the error from the calculation of the waste mass flow m ⁇ refuse completely hide or at least keep small.
  • the procedure is designed to fit into any commercial control system can be installed. It is not on any additional, special hardware or software reliant.
  • the grippers 3-10 with the weights w3-w10: w3 2950kg w4 3120kg w5 2760kg w6 2370kg w7 2590kg w8 3280kg 08:48 w9 2880kg 09:00 w10 3010kg
  • H 2 O flue gas f ( T gas _ in front _ washer . T gas _ in the _ Wäsch e r ):

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Incineration Of Waste (AREA)
  • Gasification And Melting Of Waste (AREA)

Claims (4)

  1. Procédé de réglage automatique de la combustion dans une installation d'incinération d'ordures dans laquelle la valeur thermique des ordures (Hu) est déterminée en continu à partir de la chaleur (QB) effectivement libérée dans la chambre de combustion et de l'écoulement massique d'ordures introduites (mMÜLL), caractérisé en ce que pour le réglage des grandeurs de combustion, par exemple la répartition de l'air de combustion, l'épaisseur de la couche d'ordures et la vitesse de la grille, une grandeur fictive de processus "qualité d'ordure" est déterminée à partir du pouvoir calorifique des ordures (Hu) et de la teneur en eau des ordures (H2OMÜLL), la teneur en eau des ordures (H 2OMÜLL) étant déterminée à partir de l'équation H2 OMüll = m H 2 O _ Müll m Müll dans laquelle
    m ˙H2O_Müll représente l'écoulement massique d'eau des ordures, et l'écoulement massique d'eau des ordures m ˙H2O_Müll
    étant composé de: m H 2 O _ Müll = m H 2 O _Rauchgas - m H 2 O _ Müllverbrennung m H 2 O - Öl - m H 2 O _ Verbrennungsluft dans laquelle m H2O_Rauchgan représente l'écoulement massique d'eau dans les gaz de fumée m H2O_Müllbrennung représente l'écoulement massique d'eau pendant la combustion m H2O_Öl représente l'écoulement massique d'eau provenant de la combustion supplémentaire d'huile, m H2O_Verbrennungsluft représente l'écoulement massique d'eau contenu dans l'air de combustion apporté
    et: m H 2O_Rauchgas = V Rauchgas_Kesselende·H2ORauchgas·ρH 2O_Dampf où V Rauchgas_Keselende représente l'écoulement volumique du gaz de fumée à l'extrémité de la chaudière, H2ORauchgas représente l'humidité dans le gaz de fumée, ρH2O_Dampf représente la masse volumique de l'eau sous forme de vapeur, m H 2 O _ Müllverbrennung = kH 2 O ·QB où: kH2O représente un facteur de proportionnalité, QB représente la chaleur dégagée lors de la combustion, m H 2 O _ Öl = m Öl ·AnteilH ·9,000 où : m Öl représente l'écoulement massique d'huile AnteilH représente la teneur en hydrogène dans l'huile, m H2O_Verbrennungsluft = ( V PL + V SL + V Falschluft )·H 2 OVerbrennungsluft V ˙PL
    où :
    représente l'écoulement volumique d'air primaire V SL
    représente l'écoulement volumique d'air secondaire V Falschluft
    représente l'écoulement volumique d'air parasite, H2OVerbrennungsluft
    représente le contenu dans l'air apporté à la combustion.
  2. Procédé selon la revendication 1, caractérisé en ce que l'humidité dans le gaz de fumée (H2ORAUCHGAS) est mesurée directement à l'extrémité de la chambre de combustion.
  3. Procédé selon la revendication 1, caractérisé en ce que l'humidité dans le gaz de fumée (H2ORAUCHGAS) est déterminée par l'intermédiaire de la température avant l'entrée des gaz de fumée dans un laveur de gaz de fumée raccordé en aval de l'installation d'incinération d'ordures et par l'intermédiaire de la température de saturation des gaz de fumée dans le laveur de gaz de fumée.
  4. Procédé selon l'une des revendications 2 ou 3, caractérisé en ce que la constante de proportionnalité kH2O est déterminée par l'intermédiaire d'une équation statistique écoulement massique de dioxyde de carbone mCO2=kCO2 * QB, et le rapport carbone/hydrogène (C/H) dans les ordures, k CO2 étant une constante de proportionnalité entre la chaleur dégagée (QB) et l'écoulement massique de dioxyde de carbone (mCO2).
EP00105630A 1999-04-19 2000-03-16 Procédé pour le réglage automatique de la combustion d'un incinerateur d'ordures Expired - Lifetime EP1046861B1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE19917572A DE19917572A1 (de) 1999-04-19 1999-04-19 Verfahren zur automatischen Einstellung der Feuerung einer Müllverbrennungsanlage
DE19917572 1999-04-19

Publications (2)

Publication Number Publication Date
EP1046861A1 EP1046861A1 (fr) 2000-10-25
EP1046861B1 true EP1046861B1 (fr) 2003-09-03

Family

ID=7905037

Family Applications (1)

Application Number Title Priority Date Filing Date
EP00105630A Expired - Lifetime EP1046861B1 (fr) 1999-04-19 2000-03-16 Procédé pour le réglage automatique de la combustion d'un incinerateur d'ordures

Country Status (7)

Country Link
EP (1) EP1046861B1 (fr)
JP (1) JP2000314516A (fr)
KR (1) KR100494862B1 (fr)
AT (1) ATE249011T1 (fr)
DE (2) DE19917572A1 (fr)
NO (1) NO318569B1 (fr)
TW (1) TW419575B (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7640872B2 (en) 2004-10-14 2010-01-05 Martin GmbH für Umwelt- und Energietechnik Process for influencing the properties of combustion residue

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CH694823A5 (de) * 2000-12-08 2005-07-29 Von Roll Umwelttechnik Ag Verfahren zum Betreiben einer Müllverbrennungsanlage.
JP4216731B2 (ja) * 2002-03-18 2009-01-28 イー．イー．アール． エンバイロメンタル エナジー リソースィズ （イスラエル） リミテッド 廃棄物処理装置のための制御システム
DE10330376B4 (de) * 2003-07-04 2007-09-13 Pfister Gmbh Verfahren und Vorrichtung zur kontinuierlichen, gravimetrischen Dosierung von fließfähigen Gütern für Feuerungsanlagen
DE102006005464B3 (de) 2006-02-07 2007-07-05 Forschungszentrum Karlsruhe Gmbh Verfahren zur primärseitigen Stickoxidminderung in einem zweistufigen Verbrennungsprozess
DE102007055168A1 (de) * 2007-11-19 2009-05-20 Siemens Ag Österreich Verfahren zur Regelung einer Festbrennstoff-Befeuerungseinrichtung
IT1402556B1 (it) * 2010-11-08 2013-09-13 Amsa S P A Societa Per Azioni Con Socio Unico Sistema di controllo del carico e della combustione, per impianti di combustione dei rifiuti.
FR2975463B1 (fr) * 2011-05-19 2017-02-24 Weiss France Dispositif et procede de regulation de la combustion d'une chaudiere a biomasse
JP5996762B1 (ja) * 2015-11-19 2016-09-21 株式会社タクマ 廃棄物の燃焼制御方法およびこれを適用した燃焼制御装置
DE102020124544A1 (de) 2020-09-21 2022-03-24 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung eingetragener Verein Verfahren und Anlage zum thermischen Verwerten von festem Brennstoff in einem Reaktionsraum

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6038610B2 (ja) * 1981-04-09 1985-09-02 株式会社クボタ 焼却炉の自動制御方法
JPS59183210A (ja) * 1983-04-01 1984-10-18 Takuma Co Ltd スト−カ速度制御方法
DE3537945A1 (de) 1985-10-25 1987-04-30 Babcock Anlagen Ag Verfahren zur verbrennung von abfall
ATE76957T1 (de) * 1987-10-24 1992-06-15 Mindermann Kurt Henry Verfahren zum steuern der verbrennung von brennstoff mit stark schwankendem heizwert.
DE3825931A1 (de) 1988-07-29 1990-02-01 Martin Umwelt & Energietech Verfahren und vorrichtung zur regelung der feuerungsleistung von verbrennungsanlagen
JPH0739854B2 (ja) * 1990-03-27 1995-05-01 日本鋼管株式会社 焼却用廃棄物の供給量計測方法
JPH04371712A (ja) * 1991-06-21 1992-12-24 Mitsubishi Heavy Ind Ltd ごみ焼却炉の燃焼制御方法
DE4445954A1 (de) 1994-12-22 1996-06-27 Abb Management Ag Verfahren zur Verbrennung von Abfällen
DE4446022A1 (de) * 1994-12-22 1996-06-27 Abb Patent Gmbh Verfahren und Vorrichtung zur Verbrennung von Abfällen
EP0766042A1 (fr) * 1995-09-29 1997-04-02 FINMECCANICA S.p.A. AZIENDA ANSALDO Système pour contrÔler automatiquement l'alimentation d'une substance basique à une chambre de combustion
DE19547258A1 (de) * 1995-12-06 1997-10-16 Hartmann & Braun Ag Verfahren zum Betrieb einer Müll-Verbrennungsanlage, insbesondere einer Abfall- oder Müllverbrennungsanlage
JP3822328B2 (ja) * 1997-09-26 2006-09-20 住友重機械工業株式会社 ごみ焼却炉の燃焼ごみ低位発熱量推定方法

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7640872B2 (en) 2004-10-14 2010-01-05 Martin GmbH für Umwelt- und Energietechnik Process for influencing the properties of combustion residue

Also Published As

Publication number Publication date
ATE249011T1 (de) 2003-09-15
DE50003500D1 (de) 2003-10-09
DE19917572A1 (de) 2000-10-26
NO20002080L (no) 2000-10-20
KR20000071727A (ko) 2000-11-25
TW419575B (en) 2001-01-21
EP1046861A1 (fr) 2000-10-25
NO318569B1 (no) 2005-04-11
JP2000314516A (ja) 2000-11-14
NO20002080D0 (no) 2000-04-19
KR100494862B1 (ko) 2005-06-14

Similar Documents

Publication Publication Date Title
EP0317731B1 (fr) Procédé de contrôle de la combustion de carburant possédant un pouvoir calorifique fortement variable
EP1046861B1 (fr) Procédé pour le réglage automatique de la combustion d'un incinerateur d'ordures
DE4344906C2 (de) Verfahren zum Regeln einzelner oder sämtlicher die Verbrennung auf einem Feuerungsrost beeinflussender Faktoren
DE19820038C2 (de) Verfahren zum Regeln der Feuerleistung von Verbrennungsanlagen
EP0718553A1 (fr) Méthode pour combustion d'ordures
DE69219513T2 (de) Methode und Einrichtung zur Feststellung einer unverbrannten Komponentemenge in der Asche einer kohlengefeuerten Kessels
EP0696708A1 (fr) Méthode de régulation de la combustion pour installations de combustion, notammement d'installations d'incinérations de déchets
EP1340019B1 (fr) Procede permettant de faire fonctionner une installation d'incineration d'ordures menageres
DE102018105185A1 (de) Verfahren zur Brenngasartenerkennung bei einem brenngasbetriebenen Heizgerät
CH654395A5 (de) Verfahren und anlage zur versorgung mehrerer brenner einer feuerungsanlage mit koernigem oder pulverfoermigem brennstoff.
EP0499976B1 (fr) Procédé pour fonctionnement d'une installation d'incinération
DE3423946A1 (de) Regelverfahren fuer die verbrennungsluftmenge einer feuerungseinrichtung
DE102007055168A1 (de) Verfahren zur Regelung einer Festbrennstoff-Befeuerungseinrichtung
DE69727717T2 (de) Verfahren zur Verbrennungsregelung eines Abfallverbrennungsofens
DE4446022A1 (de) Verfahren und Vorrichtung zur Verbrennung von Abfällen
EP1851481A1 (fr) Procede pour augmenter le debit de futs d'emballage dans des installations a chambre tournante
DE20221944U1 (de) Vorrichtung zum Überwachen und Erkennen eines Betriebszustands bei Brennwertheizgeräten
EP1516544B1 (fr) Dispositif et procédé de séchage pour tabac
DE19947979A1 (de) Befüllvorrichtung für Schüttgut oder Fasermaterial
EP1235029A1 (fr) Procédé d'incinération utilisant une grille et adapté à tout type de combustible
DE60028833T2 (de) Ein verfahren zur verbrennung vom festbrennstoff
EP2324289A2 (fr) Procédé et dispositif pour transporter des résidus de combustion
DE3804853A1 (de) Anlage zum verschwelen von abfallstoffen
DE2920123C2 (de) Verfahren zur Steuerung einer Fördereinrichtung zur pneumatischen Förderung von Schüttgütern
DE102024000723A1 (de) Verfahren zum Trocknen von Kunststoffmaterial sowie Anlage zur Durchführung des Verfahrens

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 CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE

AX Request for extension of the european patent

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

17P Request for examination filed

Effective date: 20010421

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

Owner name: ALSTOM (SCHWEIZ) AG

AKX Designation fees paid

Free format text: AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE

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

Owner name: ALSTOM (SWITZERLAND) LTD

GRAH Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOS IGRA

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

Owner name: MARTIN GMBH FUER UMWELT-UND ENERGIETECHNIK

GRAH Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOS IGRA

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

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

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

Effective date: 20030903

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: 20030903

Ref country code: GB

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: 20030903

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: 20030903

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: 20030903

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

REF Corresponds to:

Ref document number: 50003500

Country of ref document: DE

Date of ref document: 20031009

Kind code of ref document: P

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

Free format text: GERMAN

REG Reference to a national code

Ref country code: CH

Ref legal event code: NV

Representative=s name: MICHELI & CIE INGENIEURS-CONSEILS

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: 20031203

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: 20031203

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: 20031203

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

Effective date: 20040203

GBV Gb: ep patent (uk) treated as always having been void in accordance with gb section 77(7)/1977 [no translation filed]

Effective date: 20030903

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: 20040316

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: 20040331

Ref country code: MC

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

Effective date: 20040331

REG Reference to a national code

Ref country code: IE

Ref legal event code: FD4D

ET Fr: translation filed
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: 20040604

BERE Be: lapsed

Owner name: *MARTIN G.M.B.H. FUR UMWELT- UND ENERGIETECHNIK

Effective date: 20040331

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 17

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 18

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 19

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

Ref country code: FR

Payment date: 20190322

Year of fee payment: 20

Ref country code: IT

Payment date: 20190325

Year of fee payment: 20

Ref country code: DE

Payment date: 20190321

Year of fee payment: 20

Ref country code: CH

Payment date: 20190320

Year of fee payment: 20

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

Ref country code: NL

Payment date: 20190320

Year of fee payment: 20

Ref country code: AT

Payment date: 20190321

Year of fee payment: 20

REG Reference to a national code

Ref country code: DE

Ref legal event code: R071

Ref document number: 50003500

Country of ref document: DE

REG Reference to a national code

Ref country code: NL

Ref legal event code: MK

Effective date: 20200315

REG Reference to a national code

Ref country code: AT

Ref legal event code: MK07

Ref document number: 249011

Country of ref document: AT

Kind code of ref document: T

Effective date: 20200316