EP0246943B1 - Verfahren und Anlage, um das Umlaufen von Flüssigkeiten durch Pumpen zu fördern - Google Patents

Verfahren und Anlage, um das Umlaufen von Flüssigkeiten durch Pumpen zu fördern Download PDF

Info

Publication number
EP0246943B1
EP0246943B1 EP87401004A EP87401004A EP0246943B1 EP 0246943 B1 EP0246943 B1 EP 0246943B1 EP 87401004 A EP87401004 A EP 87401004A EP 87401004 A EP87401004 A EP 87401004A EP 0246943 B1 EP0246943 B1 EP 0246943B1
Authority
EP
European Patent Office
Prior art keywords
pump
turbine
fluid
outlet
intake
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
EP87401004A
Other languages
English (en)
French (fr)
Other versions
EP0246943A1 (de
Inventor
Claude Lepert
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.)
Ets Pompes Guinard Dite Ste
Original Assignee
Ets Pompes Guinard Dite Ste
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 Ets Pompes Guinard Dite Ste filed Critical Ets Pompes Guinard Dite Ste
Priority to AT87401004T priority Critical patent/ATE54718T1/de
Publication of EP0246943A1 publication Critical patent/EP0246943A1/de
Application granted granted Critical
Publication of EP0246943B1 publication Critical patent/EP0246943B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/12Methods or apparatus for controlling the flow of the obtained fluid to or in wells
    • E21B43/121Lifting well fluids
    • E21B43/129Adaptations of down-hole pump systems powered by fluid supplied from outside the borehole
    • EFIXED CONSTRUCTIONS
    • E21EARTH OR ROCK DRILLING; MINING
    • E21BEARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/34Arrangements for separating materials produced by the well
    • E21B43/40Separation associated with re-injection of separated materials
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D13/00Pumping installations or systems
    • F04D13/02Units comprising pumps and their driving means
    • F04D13/04Units comprising pumps and their driving means the pump being fluid driven

Definitions

  • the present invention relates to methods and installations for circulating fluids by pumping. More particularly, the invention relates to methods and installations for pumping fluids of high viscosity, for example heavy crude oils which are viscous and the pumping of which is very difficult with centrifugal hydraulics.
  • the liquid thus serves as the supply fluid for the turbine of the turbomachine providing the energy necessary for the operation of the pump.
  • the liquid also serves to reduce the viscosity of the fluid and thus make it acceptable so that the mixture of fluid and liquid can be pumped by centrifugal hydraulics.
  • the method is particularly useful in the case of a borehole, where the liquid must be sent anyway to the bottom of the borehole where the turbomachine is located, it is immediately accessible there, without the need for a pipe. special to bring him there.
  • the volume flow rate of the liquid sent to the inlet of the turbine represents from 0.5 to 3 times the volume flow rate of the fluid to be pumped. It is advantageous that the volume flow rate of the liquid mixed with the fluid to be pumped represents from 0.1 to 0.5 times the volume flow rate of the fluid to be pumped.
  • the liquid should have a low viscosity, be miscible with the fluid by reducing the viscosity of the mixture, contain little gas and preferably do not react on the fluid.
  • a liquid having a viscosity of 1 to 10 centistokes is used, having a mixture whose viscosity is less than 30 centistokes.
  • the method consists in separating the fluid which leaves the pump, in a first liquid stream and in the second stream, in compressing the first stream, in compressing the part of the expanded liquid which leaves the turbine and which does not is not mixed with the fluid and combine it with the first compressed current to send everything to the turbine inlet.
  • the invention also relates to a pumping installation, comprising a liquid source and a turbomachine comprising a pump having an inlet and an outlet, and a turbine which is stalled on the same shaft as the pump and which has an inlet and an outlet, characterized in that the outlet of the turbine opens into a conduit putting the source in communication with the pump and the installation comprises apparatus for separating a fluid into a first less viscous stream and into a second more viscous stream, the switchgear being provided with an inlet which communicates with the outlet of the pump, and two outlets one of which for the first current communicates with the inlet of the turbine and there is provided a conduit putting in communication the outlet of the turbine and the outlet of the apparatus intended for the first current, a compression pump being mounted on this conduit.
  • Fluid of high viscosity leaves a source 1 through a conduit 2.
  • a conduit 2 opens a conduit 3 coming from the outlet 4 of a turbine 5 of a turbomachine
  • This machine essentially comprises the turbine having the outlet 4 and a inlet 6 and a pump 7 having an inlet 8 and an outlet 9 and wedged on the same shaft 10 as the turbine 5.
  • a detailed description of this turbomachine can be found in patent FR-A 2 433 117.
  • the mixture of viscous fluid and less viscous liquid is sent under a pressure of between 10 and 150 bar, via a conduit 11 at the inlet of the pump 7.
  • the latter discharges it through the outlet 9 and through a conduit 12 into a separation apparatus 13 where the mixture, optionally after settling or centrifugation of the solid materials, is separated into a first stream going through the conduit 14, with compression in a pump 16 at a pressure between 20 and 300 bar, at the inlet 6 of the turbine 5 and in a second stream discharged through a pipe 15.
  • the additional liquid which leaves the turbine and which is not sent to the inlet of the pump is returned by a pipe 17, passing through a pump 18 which puts it under a pressure of between 20 and 300 bar, to a conduit 19 which joins the conduit leaving the pump 16 and going to the inlet of the turbine.

Landscapes

  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Mining & Mineral Resources (AREA)
  • Geology (AREA)
  • Fluid Mechanics (AREA)
  • Environmental & Geological Engineering (AREA)
  • Physics & Mathematics (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Jet Pumps And Other Pumps (AREA)

Claims (5)

1. Verfahren zum Pumpen eines Fluids hoher Viskosität, insbesondere schwerer Kohlenwasserstoffe oder Erdöle, bei welchem eine Flüssigkeit mit einer geringeren Viskosität als die des Fluids, die mit diesem mischbar ist, unter Druck dem Eingang (6) der Turbine (5) einer Strömungsmaschine zugeführt .wird, die eine Pumpe (7) umfaßt mit einem Eingang (8) und einem Ausgang (9) sowie eine Turbine (5), die einen Eingang (6) und einen Ausgang (4), welche von denen der Pumpe verschieden sind, aufweist und die auf der gleichen Welle (10) befestigt ist wie die Pumpe, dadurch gekennzeichnet, daß ein Teil der entspannten Flüssigkeit der aus der Turbine kommt, dem Fluid zugemischt wird und daß die Mischung der entspannten Flüssigkeit und des Fluids vom Eingang der Pumpe angesaugt wird.
2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß die Volumenmenge der in die Turbine geleiteten Flüssigkeit die 0,5- bis 3-fache Volumenmenge des zu pumpenden Fluids bildet.
3. Verfahren nach Anspruch 1 oder 2, dadurch gekennzeichnet, daß die Volumenmenge der dem Fluid zugemischten Flüssigkeit die 0,1- bis 0,5-fache Volumenmenge des Fluids bildet.
4. Verfahren nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß das Fluid, welches die Pumpe verläßt, in einen ersten flüssigen Strom und in einen zweiten Strom getrennt wird, daß der erste Strom komprimiert wird, daß der Teil der entspannten Flüssigkeit, der von der Turbine kommt und nicht dem Fluid beigemischt wird, komprimiert wird und mit dem ersten, komprimierten Strom vereinigt wird um das Ganze zum Eingang der Turbine zu leiten.
5. Pumpenanlage, bestehend aus einer Flüssigkeitsquelle (1) und einer Strömungsmaschine bestehend aus einer Pumpe (7), die einen Eingang (8) und einen Ausgang (9) aufweist und einer Turbine (5), die auf der gleichen Welle befestigt ist, wie die Pumpe (7) und die einen Eingang (6) und einen Ausgang (4) aufweist, dadurch gekennzeichnet, daß der Ausgang (4) der Turbine (5) in eine Leitung (11) mündet, die die Quelle (1) mit der Pumpe (7) verbindet, wobei die Anlage eins Trennapparatur (13) aufweist zur Trennung eines Fluids in einen ersten, weniger viskosen Strom (14) und in einen zweiten stärker viskosen Strom (15), wobei die Apparatur mit einem Eingang (12), der in Verbindung steht mit dem Ausgang der Pumpe (7), und mit zwei Ausgängen versehen ist, von denen der eine für den ersten Strom mit dem Eingang (6) der Turbine verbunden ist, und daß eine Leitung (17) vorgesehen ist, die den Ausgang (4) der Turbine und den Ausgang der Apparatur (13), der für den ersten Strom bestimmt ist, verbindet, wobei eine Druckpumpe in diese Leitung (17) eingeschaltet ist.
EP87401004A 1986-05-21 1987-04-30 Verfahren und Anlage, um das Umlaufen von Flüssigkeiten durch Pumpen zu fördern Expired - Lifetime EP0246943B1 (de)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT87401004T ATE54718T1 (de) 1986-05-21 1987-04-30 Verfahren und anlage, um das umlaufen von fluessigkeiten durch pumpen zu foerdern.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8607204A FR2599091B1 (fr) 1986-05-21 1986-05-21 Procede et installation pour faire circuler des fluides par pompage
FR8607204 1986-05-21

Publications (2)

Publication Number Publication Date
EP0246943A1 EP0246943A1 (de) 1987-11-25
EP0246943B1 true EP0246943B1 (de) 1990-07-18

Family

ID=9335425

Family Applications (1)

Application Number Title Priority Date Filing Date
EP87401004A Expired - Lifetime EP0246943B1 (de) 1986-05-21 1987-04-30 Verfahren und Anlage, um das Umlaufen von Flüssigkeiten durch Pumpen zu fördern

Country Status (9)

Country Link
US (1) US4721436A (de)
EP (1) EP0246943B1 (de)
JP (1) JPS62279296A (de)
AT (1) ATE54718T1 (de)
CA (1) CA1274418A (de)
DE (1) DE3763746D1 (de)
ES (1) ES2016372B3 (de)
FR (1) FR2599091B1 (de)
GR (1) GR3000651T3 (de)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2680983A1 (fr) * 1991-09-10 1993-03-12 Inst Francais Du Petrole Dispositif melangeur continu, procede et utilisation dans une installation de pompage d'un fluide de forte viscosite.
DE4243132C1 (de) * 1992-12-19 1994-07-07 Klein Schanzlin & Becker Ag Turbopumpe zur Förderung hochviskoser Stoffe
US5582505A (en) * 1992-11-03 1996-12-10 Ksb Aktiengesellschaft Bore-hole pump

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5611397A (en) * 1994-02-14 1997-03-18 Wood; Steven M. Reverse Moineau motor and centrifugal pump assembly for producing fluids from a well
US5417281A (en) * 1994-02-14 1995-05-23 Steven M. Wood Reverse Moineau motor and pump assembly for producing fluids from a well
JPH0674707B2 (ja) * 1988-09-09 1994-09-21 インテベップ,エス.エイ. オイルの取出し装置とその方法
FR2656035B1 (fr) * 1989-12-15 1996-01-12 Inst Francais Du Petrole Dispositif de pompage d'un liquide et en particulier d'un liquide a forte viscosite.
US5558502A (en) * 1993-12-24 1996-09-24 Pacific Machinery & Engineering Co., Ltd. Turbo pump and supply system with the pump
GB0128262D0 (en) * 2001-11-24 2002-01-16 Rotech Holdings Ltd Artificial lift pump
US6854517B2 (en) * 2002-02-20 2005-02-15 Baker Hughes Incorporated Electric submersible pump with specialized geometry for pumping viscous crude oil
ITCO20120015A1 (it) * 2012-04-12 2013-10-13 Nuovo Pignone Srl Metodo per la prevenzione della corrosione e componente ottenuto mediante tale metodo
CN104989616A (zh) * 2015-05-28 2015-10-21 中国石油天然气股份有限公司 一种抽油泵涡轮增压器

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US975526A (en) * 1910-09-15 1910-11-15 Ernest K Hood Propeller turbine-pump.
US1842960A (en) * 1925-08-21 1932-01-26 Anna M C Wechsberg Pumping device
FR993641A (fr) * 1949-04-28 1951-11-05 Appareils de pompage pour puits profonds
US3194026A (en) * 1963-10-24 1965-07-13 Fleur Corp Power-refrigeration system
US3420434A (en) * 1966-12-30 1969-01-07 Judson S Swearingen Rotary compressors and systems employing same using compressor gas as seal gas
FR2285532A1 (fr) * 1974-09-20 1976-04-16 Kobe Inc Pompe a commande par turbine pour puits de petrole
US4003678A (en) * 1975-02-10 1977-01-18 E M C Energies, Inc. Fluid operated well turbopump
US4035023A (en) * 1975-07-15 1977-07-12 Freeport Minerals Company Apparatus and process for hydraulic mining
US4233154A (en) * 1978-12-29 1980-11-11 Kobe, Inc. Method for treating petroleum well pumping power fluid
DE3022600A1 (de) * 1979-06-21 1981-01-29 Kobe Inc Vorrichtung und verfahren zum pumpen eines bohrlochs
US4292011A (en) * 1979-08-20 1981-09-29 Kobe, Inc. Turbo pump gas compressor
US4285401A (en) * 1980-06-09 1981-08-25 Kobe, Inc. Electric and hydraulic powered thermal stimulation and recovery system and method for subterranean wells

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2680983A1 (fr) * 1991-09-10 1993-03-12 Inst Francais Du Petrole Dispositif melangeur continu, procede et utilisation dans une installation de pompage d'un fluide de forte viscosite.
EP0532397A1 (de) * 1991-09-10 1993-03-17 Institut Francais Du Petrole Kontinuierliche Mischvorrichtung, Verfahren und Verwendung in einer Pumpanlage für Fluid hoher Viskosität
US5582505A (en) * 1992-11-03 1996-12-10 Ksb Aktiengesellschaft Bore-hole pump
DE4243132C1 (de) * 1992-12-19 1994-07-07 Klein Schanzlin & Becker Ag Turbopumpe zur Förderung hochviskoser Stoffe
WO1994015065A1 (de) * 1992-12-19 1994-07-07 Ksb Aktiengesellschaft Turbopumpe zur förderung hochviskoser stoffe
US5655895A (en) * 1992-12-19 1997-08-12 Ksb Aktiengesellschaft Turbopump for conveying highly viscous substances

Also Published As

Publication number Publication date
CA1274418A (en) 1990-09-25
DE3763746D1 (de) 1990-08-23
FR2599091A1 (fr) 1987-11-27
EP0246943A1 (de) 1987-11-25
ES2016372B3 (es) 1990-11-01
US4721436A (en) 1988-01-26
GR3000651T3 (en) 1991-09-27
FR2599091B1 (fr) 1990-10-26
JPS62279296A (ja) 1987-12-04
ATE54718T1 (de) 1990-08-15

Similar Documents

Publication Publication Date Title
EP0246943B1 (de) Verfahren und Anlage, um das Umlaufen von Flüssigkeiten durch Pumpen zu fördern
CA2204664C (fr) Systeme de pompage polyphasique et centrifuge
EP0532397B1 (de) Kontinuierliche Mischvorrichtung, Verfahren und Verwendung in einer Pumpanlage für Fluid hoher Viskosität
US5084189A (en) Method and apparatus for separating fluids having different specific gravities
US6089317A (en) Cyclonic separator assembly and method
US8092692B2 (en) Apparatus and method for separating immiscible fluid components
DE68913301T2 (de) Vorrichtung zur Entfernung von Gasen aus Flüssigkeiten.
FR2526325A1 (fr) Dispositif pour la separation par tourbillonnement de liquides a densites differentes, a dechargement automatique
FR2594183A1 (fr) Procede et installation pour faire circuler des fluides par pompage
FR2570162A1 (fr) Procede et dispositif de compression et de transport d'un gaz contenant une fraction liquide
CN108862466B (zh) 一种基于轴向涡流技术进行含油污水预分离的设备和方法
FR2772636A1 (fr) Ensemble pour l'epuration automatique d'un fluide pollue et procede de mise en oeuvre
CA1053588A (en) Cleaning and pumping apparatus for oil well production
FR2679575A1 (fr) Prise d'eau, en particulier pour installation industrielle.
WO1987003051A1 (fr) Compresseur de fluide gazeux, associe a un separateur gaz-liquide
EP0513222A1 (de) Kreiselpumpenschmiermittelfiltersystem
EP0702156B1 (de) Mehrphasiges Pumpensystem mit Regelkreis
FR2635748A1 (fr) Procede de separation de l'eau des boues huileuses, lors du traitement des fuels a bord des navires
FR2528124A1 (fr) Groupe motopompe pour puits de forage et procede de protection s'y rapportant
JPH01151912A (ja) 気泡分離機能付の液体圧力調節装置
RU2387884C1 (ru) Центробежный сепаратор твердых частиц
FR2354462A1 (fr) Pompe centrifuge
EP0546489B1 (de) Vorrichtung zum Rehomogenisierung einer Gas-Flüssigkeitsmischung
JPH034907A (ja) 液体中の気泡除去システム
RU1736047C (ru) Виброкомплекс

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 DE ES FR GB GR IT LI LU NL SE

17P Request for examination filed

Effective date: 19880115

17Q First examination report despatched

Effective date: 19890330

ITF It: translation for a ep patent filed
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 DE ES FR GB GR IT LI LU NL SE

REF Corresponds to:

Ref document number: 54718

Country of ref document: AT

Date of ref document: 19900815

Kind code of ref document: T

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

Ref document number: 3763746

Country of ref document: DE

Date of ref document: 19900823

REG Reference to a national code

Ref country code: GR

Ref legal event code: FG4A

Free format text: 3000651

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
ITTA It: last paid annual fee
REG Reference to a national code

Ref country code: FR

Ref legal event code: CD

EPTA Lu: last paid annual fee
EAL Se: european patent in force in sweden

Ref document number: 87401004.4

REG Reference to a national code

Ref country code: FR

Ref legal event code: CA

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

Ref country code: AT

Payment date: 19970320

Year of fee payment: 11

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

Ref country code: GR

Payment date: 19970321

Year of fee payment: 11

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

Ref country code: ES

Payment date: 19970416

Year of fee payment: 11

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

Ref country code: SE

Payment date: 19970423

Year of fee payment: 11

Ref country code: BE

Payment date: 19970423

Year of fee payment: 11

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

Ref country code: NL

Payment date: 19970428

Year of fee payment: 11

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

Ref country code: DE

Payment date: 19970429

Year of fee payment: 11

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

Ref country code: CH

Payment date: 19970605

Year of fee payment: 11

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

Ref country code: LU

Payment date: 19970620

Year of fee payment: 11

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: 19980430

Ref country code: LI

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

Effective date: 19980430

Ref country code: GR

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

Effective date: 19980430

Ref country code: CH

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

Effective date: 19980430

Ref country code: BE

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

Effective date: 19980430

Ref country code: AT

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

Effective date: 19980430

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 NON-PAYMENT OF DUE FEES

Effective date: 19980501

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 EXPIRATION OF PROTECTION

Effective date: 19980504

BERE Be: lapsed

Owner name: ETS. POMPES GUINARD

Effective date: 19980430

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 NON-PAYMENT OF DUE FEES

Effective date: 19981101

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

NLV4 Nl: lapsed or anulled due to non-payment of the annual fee

Effective date: 19981101

EUG Se: european patent has lapsed

Ref document number: 87401004.4

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: 19990302

REG Reference to a national code

Ref country code: FR

Ref legal event code: TP

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 20000201

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

Ref country code: GB

Payment date: 20000331

Year of fee payment: 14

REG Reference to a national code

Ref country code: FR

Ref legal event code: CD

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: 20010430

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

Effective date: 20010430

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

Ref country code: IT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED.

Effective date: 20050430

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

Ref country code: FR

Payment date: 20060414

Year of fee payment: 20