EP0654138A1 - Heating apparatus. - Google Patents

Heating apparatus.

Info

Publication number
EP0654138A1
EP0654138A1 EP93918026A EP93918026A EP0654138A1 EP 0654138 A1 EP0654138 A1 EP 0654138A1 EP 93918026 A EP93918026 A EP 93918026A EP 93918026 A EP93918026 A EP 93918026A EP 0654138 A1 EP0654138 A1 EP 0654138A1
Authority
EP
European Patent Office
Prior art keywords
mandrel
heating element
liquid
heating
source
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
EP93918026A
Other languages
German (de)
French (fr)
Other versions
EP0654138B1 (en
Inventor
John Graham Hart
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of EP0654138A1 publication Critical patent/EP0654138A1/en
Application granted granted Critical
Publication of EP0654138B1 publication Critical patent/EP0654138B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H1/00Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
    • F24H1/10Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium
    • F24H1/12Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium in which the water is kept separate from the heating medium
    • F24H1/14Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium in which the water is kept separate from the heating medium by tubes, e.g. bent in serpentine form
    • F24H1/142Continuous-flow heaters, i.e. heaters in which heat is generated only while the water is flowing, e.g. with direct contact of the water with the heating medium in which the water is kept separate from the heating medium by tubes, e.g. bent in serpentine form using electric energy supply

Definitions

  • This invention relates to a method and apparatus for heating liquids, and in particular to a method of apparatus for heating liquids in an indirect manner.
  • Liquids are commonly heated by allowing them to flow over a hot surface but some fluids are very difficult to heat in this way. For example, many (such as some biological fluids) deposit layers of solid material on the heat transfer surface which then act as insulation impeding the further flow of heat to the liquid. This tendency, referred to as fouling, may be reduced to some extent by various stratagems but nevertheless remains a considerable problem.
  • the invention seeks to provide a method and apparatus of heating liquid improved in the above respects.
  • a method of heating a liquid which comprises providing a mandrel within a heating element having at least one surface, and passing the liquid down the mandrel in the form of a thin film in such a manner that it does not contact the heating surface.
  • the invention also provides an apparatus which comprises a heating element within which is located a mandrel, not in contact with the element, a source of liquid, and means for allowing the liquid from the source to flow over the mandrel in the form of a thin film.
  • the mandrel will normally be maintained in a vertical orientation and the source of liquid may be at the top thereof.
  • the liquid is allowed to run as a film down the surface of the mandrel.
  • the mandrel is surrounded by the hot surface of the heating element and heat passes principally by radiant heat across the gap between the hot surface of the heating element to the liquid passing down the mandrel, or by convection in the gas or vapour in the gap, or by a combination of both processes.
  • the mandrel will itself will normally not be heated and, indeed, it may be made from materials having good corrosion and release properties but a thermal conductivity so poor that they would not normally be used in heat exchanger manufacture. It need not be made from metal, and may, for example, be made from materials such as ceramics or glass, optionally with release coatings of, for instance, PTFE.
  • the indirect heating of the liquid has various advantages. Firstly heat transferred to the liquid continues even if a layer of solid material builds up on the mandrel over which it flows. Secondly it is envisaged that in most cases solids will not bond to the unheated mandrel in the same way that they would to a heated surface. This will result in a large proportion of any solids formed simply washing down the mandrel with the liquid and not permanently fouling the mandrel surface.
  • the apparatus can be arranged so that mandrels can be removed easily for cleaning in contrast to the tubes or plates of a conyentional process heat exchanger.
  • the heating elements may be of any suitable design and will preferably be a cylindrical element surrounding the mandrel but not touching it. Heating may be, for example, by hot oil or high pressure steam, although in certain circumstances an electrical heating element may be employed.
  • the gap between the heating element and the mandrel will be adjusted to suit the requirements of the process being carried out and may contain air or some other gas or may be evacuated.
  • the heat supplied to the fluid can simply be to increase its temperature but it is envisaged that the apparatus will be used most frequently for the purpose of evaporating some or all of the liquid. In this case vapour will be produced which will pass through the gap between the mandrel and the heating element and may leave the apparatus from the top, or with unvapourised liquid from the bottom.
  • an apparatus for heating liquids generally designated (10) comprises a central vertical mandrel (12) surrounded by a cylindrical heating element (14) , which may be an electrical heating element.
  • a gap (16) exists between the mandrel (12) and the element (14) and the element (14) .
  • a fluid reservoir (18) is provided at the top of the vertical mandrel (12) .
  • Means, such as a narrow annular gap (20) are arranged between the reservoir (18) and the mandrel (12) such that a film (22) of liquid flows downwardly over the surface of the mandrel (12) .
  • the element (14) is activated so that heat is radiated and/or convected towards the mandrel (12) .
  • the means (20) is activated to allow the film (22) to flow down the surface of the mandrel (12) .
  • the film (22) receives heat indirectly from the element (14) , that is the liquid is not in contact with any heated surface of the element (14) but receives the heat by radiation, convection or a combination of the two.
  • Hot liquid (24) is removed from the bottom of the apparatus (10) .
  • Vapour may be removed either from the top of the element (14) or from the bottom together with the heated liquid.
  • a typical mandrel diameter may be in the range of from 40 to 100 mm with a gap size in the range of from 2mm to 20 mm, but dimensions outside these ranges may be employed where appropriate.
  • the apparatus and method of the invention are particularly used with liquids which are difficult to heat without fouling, such as oils, aqueous solutions of salts, and biological fluids.
  • the apparatus of the invention may be used singly, in multiple applications, either parallel or series, or with other conventional apparatus.
  • the apparatus and method of the invention provides an improved method of heating liquids prone to fouling.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Instantaneous Water Boilers, Portable Hot-Water Supply Apparatuses, And Control Of Portable Hot-Water Supply Apparatuses (AREA)

Abstract

A method of heating a liquid which comprises providing a mandrel (12) within a heating element (14) having at least one surface, and passing the liquid down the mandrel in the form of a thin film (22) in such a manner that it does not contact the heating surface (14). This may be carried out in apparatus which comprises a heating element (14) within which is located a mandrel (12), not in contact with the element, a source of liquid (18), and means (20) for allowing the liquid from the source to flow over the mandrel (12) in the form of a thin film (22). The mandrel (12) will normally be maintained in a vertical orientation and the source of liquid (18) may be at the top thereof. The liquid is allowed to run as a film (22) down the surface of the mandrel (12). The mandrel (12) is surrounded by the hot surface of the heating element (14) and heat passes principally by radiant heat across the gap (16) between the hot surface of the heating element (14) to the liquid passing down the mandrel (12). Thus there is no direct contact between the liquid to be heated and any heated surface of the heating element (14). The mandrel (12) itself will normally not be heated and, indeed, it may be made from materials having good corrosion and release properties but a thermal conductivity so poor that they would not normally be used in heat exchanger manufacture. It need not be made from metal, and may, for example, be made from materials such as ceramics or glass, optionally with release coatings of, for instance, PTFE.

Description

HEATING APPARATUS
This invention relates to a method and apparatus for heating liquids, and in particular to a method of apparatus for heating liquids in an indirect manner.
Liquids are commonly heated by allowing them to flow over a hot surface but some fluids are very difficult to heat in this way. For example, many (such as some biological fluids) deposit layers of solid material on the heat transfer surface which then act as insulation impeding the further flow of heat to the liquid. This tendency, referred to as fouling, may be reduced to some extent by various stratagems but nevertheless remains a considerable problem.
The invention seeks to provide a method and apparatus of heating liquid improved in the above respects.
According to the present invention there is provided a method of heating a liquid which comprises providing a mandrel within a heating element having at least one surface, and passing the liquid down the mandrel in the form of a thin film in such a manner that it does not contact the heating surface.
The invention also provides an apparatus which comprises a heating element within which is located a mandrel, not in contact with the element, a source of liquid, and means for allowing the liquid from the source to flow over the mandrel in the form of a thin film.
The mandrel will normally be maintained in a vertical orientation and the source of liquid may be at the top thereof. The liquid is allowed to run as a film down the surface of the mandrel. The mandrel is surrounded by the hot surface of the heating element and heat passes principally by radiant heat across the gap between the hot surface of the heating element to the liquid passing down the mandrel, or by convection in the gas or vapour in the gap, or by a combination of both processes. Thus there is no direct contact between the liquid to be heated and any heated surface of the heating element. The mandrel will itself will normally not be heated and, indeed, it may be made from materials having good corrosion and release properties but a thermal conductivity so poor that they would not normally be used in heat exchanger manufacture. It need not be made from metal, and may, for example, be made from materials such as ceramics or glass, optionally with release coatings of, for instance, PTFE.
The indirect heating of the liquid has various advantages. Firstly heat transferred to the liquid continues even if a layer of solid material builds up on the mandrel over which it flows. Secondly it is envisaged that in most cases solids will not bond to the unheated mandrel in the same way that they would to a heated surface. This will result in a large proportion of any solids formed simply washing down the mandrel with the liquid and not permanently fouling the mandrel surface. The apparatus can be arranged so that mandrels can be removed easily for cleaning in contrast to the tubes or plates of a conyentional process heat exchanger.
The heating elements may be of any suitable design and will preferably be a cylindrical element surrounding the mandrel but not touching it. Heating may be, for example, by hot oil or high pressure steam, although in certain circumstances an electrical heating element may be employed. The gap between the heating element and the mandrel will be adjusted to suit the requirements of the process being carried out and may contain air or some other gas or may be evacuated.
The heat supplied to the fluid can simply be to increase its temperature but it is envisaged that the apparatus will be used most frequently for the purpose of evaporating some or all of the liquid. In this case vapour will be produced which will pass through the gap between the mandrel and the heating element and may leave the apparatus from the top, or with unvapourised liquid from the bottom.
The invention will be described further, by way of example, with reference to the accompanying drawing in which the sole figure is a diagrammatic sectional view of an apparatus in accordance with the invention.
Referring to the drawing, an apparatus for heating liquids generally designated (10) comprises a central vertical mandrel (12) surrounded by a cylindrical heating element (14) , which may be an electrical heating element. A gap (16) exists between the mandrel (12) and the element (14) and the element (14) . A fluid reservoir (18) is provided at the top of the vertical mandrel (12) . Means, such as a narrow annular gap (20) , are arranged between the reservoir (18) and the mandrel (12) such that a film (22) of liquid flows downwardly over the surface of the mandrel (12) .
In use, the element (14) is activated so that heat is radiated and/or convected towards the mandrel (12) . The means (20) is activated to allow the film (22) to flow down the surface of the mandrel (12) . The film (22) receives heat indirectly from the element (14) , that is the liquid is not in contact with any heated surface of the element (14) but receives the heat by radiation, convection or a combination of the two. Hot liquid (24) is removed from the bottom of the apparatus (10) .
Should it be required to vaporise some or all of the liquid then the rate of flow of the liquid and/or the amount of heat provided by the element (14) is adjusted so that the necessary evaporation takes place. Vapour may be removed either from the top of the element (14) or from the bottom together with the heated liquid.
For the majority of applications a typical mandrel diameter may be in the range of from 40 to 100 mm with a gap size in the range of from 2mm to 20 mm, but dimensions outside these ranges may be employed where appropriate.
The apparatus and method of the invention are particularly used with liquids which are difficult to heat without fouling, such as oils, aqueous solutions of salts, and biological fluids. The apparatus of the invention may be used singly, in multiple applications, either parallel or series, or with other conventional apparatus.
The apparatus and method of the invention provides an improved method of heating liquids prone to fouling.

Claims

1. A method of heating a liquid which comprises providing a mandrel within a heating element having at least one surface, and passing the liquid down the mandrel in the form of a thin film in such a manner that it does not contact the heating surface.
2. An apparatus which comprises a heating element within which is located a mandrel, not in contact with the element, a source of liquid, and means for allowing the liquid from the source to flow over the mandrel in the form of a thin film.
3. An apparatus as claimed in claim 2 wherein the mandrel is maintained in a vertical orientation and the source of liquid is at the top thereof.
4. An apparatus as claimed in claim 3 in which the hot surface of the heating element surrounds the mandrel and heat passes principally by radiant heat across the gap between the hot surface of the heating element to the liquid passing down the mandrel.
5. An apparatus as claimed in claim 3 in which the hot surface of the heating element surrounds the mandrel and heat passes principally by convection in the gas or vapour in the gap between the hot surface of the heating element to the liquid passing down the mandrel.
6. An apparatus as claimed in any of claims 2 to 5 in which the mandrel is not itself heated.
7. An apparatus as claimed in claim 6 in which the mandrel is made from a material having good corrosion and release properties but of low thermal conductivity.
8. An apparatus as claimed in claim 7 in which the mandrel is made from a ceramic or glass.
9. An apparatus as claimed in claim 8 in which the mandrel iscoated with a release coating.
10. An apparatus as claimed in any of claims 2 to 9 wherein the mandrel is easily removable for cleaning.
11. An apparatus as claimed in any of claims 2 to 10 in which the heating element is a cylindrical element surrounding the mandrel but not touching it.
12. An apparatus as claimed in in claim 11 in which the heating element is heated by hot oil, high pressure steam, or an electrical heating element.
13. An apparatus as claimed in any of claims 2 to 11 in which the gap between the heating element and the mandrel is from 2mm to 20 mm.
AMENDED CLAIMS
[received by the International Bureau on 3 February 1994 (03.02.94); original claim 6 cancelled; original claims 1,2 and 7 amended; other claims unchanged (2 pages)]
1. A method of heating a liquid which comprises providing an unheated mandrel within a heating element having at least one heating surface, and passing the liquid down the mandrel in the form of a thin film in such a manner that it does not contact the heating surface.
2. An apparatus which comprises a heating element within which is located an unheated mandrel, not in contact with the element, a source of liquid, and means for allowing the liquid from the source to flow over the mandrel in the form of a thin film.
3. An apparatus as claimed in claim 2 wherein the mandrel is maintained in a vertical orientation and the source of liquid is at the top thereof.
4. An apparatus as claimed in claim 3 in which the hot surface of the heating element surrounds the mandrel and heat passes principally by radiant heat across the gap between the hot surface of the heating element to the liquid passing down the mandrel.
5. An apparatus as claimed in claim 3 in which the hot surface of the heating element surrounds the mandrel and heat passes principally by convection in the gas or vapour in the gap between the hot surface of the heating element to the liquid passing down the mandrel.
6. (Deleted)
7. An apparatus as claimed in any of claims 2 to 5 in which the mandrel is made from a material having good corrosion and release properties but of low thermal conductivity. 8. An apparatus as claimed in claim 7 in which the mandrel is made from a ceramic or glass.
9. An apparatus as claimed in claim 8 in which the mandrel iscoated with a release coating.
10. An apparatus as claimed in any of claims 2 to 9 wherein the mandrel is easily removable for cleaning.
11. An apparatus as claimed in any of claims 2 to 10 in which the heating element is a cylindrical element surrounding the mandrel but not touching it.
12. An apparatus as claimed in in claim 11 in which the heating element is heated by hot oil, high pressure steam, or an electrical heating element.
13. An apparatus as claimed in any of claims 2 to 11 in which the gap between the heating element and the mandrel is from 2mm to 20 mm.
EP93918026A 1992-08-13 1993-08-13 Heating apparatus Expired - Lifetime EP0654138B1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GB929217176A GB9217176D0 (en) 1992-08-13 1992-08-13 Heating apparatus
GB9217176 1992-08-13
PCT/GB1993/001728 WO1994004876A1 (en) 1992-08-13 1993-08-13 Heating apparatus

Publications (2)

Publication Number Publication Date
EP0654138A1 true EP0654138A1 (en) 1995-05-24
EP0654138B1 EP0654138B1 (en) 1996-12-04

Family

ID=10720274

Family Applications (1)

Application Number Title Priority Date Filing Date
EP93918026A Expired - Lifetime EP0654138B1 (en) 1992-08-13 1993-08-13 Heating apparatus

Country Status (8)

Country Link
EP (1) EP0654138B1 (en)
JP (1) JPH08500895A (en)
AU (1) AU4726293A (en)
CA (1) CA2142291A1 (en)
DE (1) DE69306395T2 (en)
ES (1) ES2094559T3 (en)
GB (1) GB9217176D0 (en)
WO (1) WO1994004876A1 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6607607B2 (en) 2000-04-28 2003-08-19 Bj Services Company Coiled tubing wellbore cleanout

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB384090A (en) * 1931-01-26 1932-12-01 Eloy Cignolo Apparatus for heating gases by electricity
CH604798A5 (en) * 1976-06-18 1978-09-15 Bertrams Ag Hch

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO9404876A1 *

Also Published As

Publication number Publication date
GB9217176D0 (en) 1992-09-23
DE69306395D1 (en) 1997-01-16
AU4726293A (en) 1994-03-15
WO1994004876A1 (en) 1994-03-03
JPH08500895A (en) 1996-01-30
DE69306395T2 (en) 1997-07-10
CA2142291A1 (en) 1994-03-03
EP0654138B1 (en) 1996-12-04
ES2094559T3 (en) 1997-01-16

Similar Documents

Publication Publication Date Title
CA2101439A1 (en) Fluid heater
KR20040074989A (en) Vaporizer/delivery vessel for volatile/thermally sensitive solid and liquid compounds
EP2536868B1 (en) Heating system for a vapor-phase deposition source
JPS63108712A (en) Method and apparatus for heating semiconductor substrate and for inducing reaction
SE8200970L (en) PROCEDURE AND DEVICE FOR CONTINUOUS DRYING OF A POROS COAT OF PAPER OR SIMILAR
KR910004296A (en) Synthetic diamond coating device comprising curved filaments and substrate cooling means
US2279000A (en) Art of cooking
CA2210115A1 (en) Vaporizer and liquid delivery system using same
Dewangan et al. Experimental study of nucleate boiling heat transfer of R-134a and R-600a on thermal spray coating surfaces
DE3661575D1 (en) Heating cylinder for products such as films, foils, slabs or the like
US3203404A (en) Water heater with heat insulating coating on tubes
US2360665A (en) Apparatus for heat extraction
EP0654138B1 (en) Heating apparatus
US2759328A (en) Pressurized heater for producing hot process water in large quantities from scale-forming water
JPH11340190A (en) Cooling/heating device for semiconductor processing liquid
CN111288247B (en) Dome stress isolation layer
TW201615377A (en) Cooling roll and method for manufacturing same
JPH11116278A (en) Production of fluororesin coated body
KR20050055714A (en) Processes for redistributing heat flux on process tubes within process heaters, and process heaters including the same
US1996852A (en) Process and apparatus for distilling or expelling volatile constituents from liquids
TWI419989B (en) Combined type crucible
US1403471A (en) Method of heating at high temperatures
GB2190687A (en) A heater
US1864349A (en) Method of evaporating liquids
GB1202936A (en) The heating or cooling of corrosive liquids

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

17P Request for examination filed

Effective date: 19950310

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): BE DE ES FR GB IT NL SE

GRAG Despatch of communication of intention to grant

Free format text: ORIGINAL CODE: EPIDOS AGRA

17Q First examination report despatched

Effective date: 19960117

GRAH Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOS IGRA

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): BE DE ES FR GB IT NL SE

REF Corresponds to:

Ref document number: 69306395

Country of ref document: DE

Date of ref document: 19970116

REG Reference to a national code

Ref country code: ES

Ref legal event code: FG2A

Ref document number: 2094559

Country of ref document: ES

Kind code of ref document: T3

ITF It: translation for a ep patent filed

Owner name: STUDIO TORTA SOCIETA' SEMPLICE

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
REG Reference to a national code

Ref country code: GB

Ref legal event code: IF02

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

Ref country code: NL

Payment date: 20060803

Year of fee payment: 14

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

Ref country code: FR

Payment date: 20060808

Year of fee payment: 14

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

Ref country code: IT

Payment date: 20060831

Year of fee payment: 14

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

Ref country code: SE

Payment date: 20060804

Year of fee payment: 14

EUG Se: european patent has lapsed
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: 20070814

Ref country code: NL

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

Effective date: 20080301

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

Effective date: 20080301

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

Effective date: 20080430

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

Ref country code: FR

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

Effective date: 20070831

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

Ref country code: GB

Payment date: 20080820

Year of fee payment: 16

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

Ref country code: ES

Payment date: 20090220

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: 20090227

Year of fee payment: 16

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

Ref country code: BE

Payment date: 20090119

Year of fee payment: 16

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

Effective date: 20070813

BERE Be: lapsed

Owner name: *HART JOHN GRAHAM

Effective date: 20090831

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

Effective date: 20090813

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: 20090831

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: 20100302

REG Reference to a national code

Ref country code: ES

Ref legal event code: FD2A

Effective date: 20090814

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: 20090813

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: 20090814