EP0409904B1 - A discharge apparatus - Google Patents

A discharge apparatus Download PDF

Info

Publication number
EP0409904B1
EP0409904B1 EP19890906122 EP89906122A EP0409904B1 EP 0409904 B1 EP0409904 B1 EP 0409904B1 EP 19890906122 EP19890906122 EP 19890906122 EP 89906122 A EP89906122 A EP 89906122A EP 0409904 B1 EP0409904 B1 EP 0409904B1
Authority
EP
European Patent Office
Prior art keywords
container
gas
elements
outlet
conduit
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
EP19890906122
Other languages
German (de)
French (fr)
Other versions
EP0409904A1 (en
Inventor
Jan-Peter BJÖRKLUND
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.)
Partek Oy AB
Raute Dry Mix Oy
Original Assignee
Partek Oy AB
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 Partek Oy AB filed Critical Partek Oy AB
Priority to AT89906122T priority Critical patent/ATE97380T1/en
Publication of EP0409904A1 publication Critical patent/EP0409904A1/en
Application granted granted Critical
Publication of EP0409904B1 publication Critical patent/EP0409904B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65DCONTAINERS FOR STORAGE OR TRANSPORT OF ARTICLES OR MATERIALS, e.g. BAGS, BARRELS, BOTTLES, BOXES, CANS, CARTONS, CRATES, DRUMS, JARS, TANKS, HOPPERS, FORWARDING CONTAINERS; ACCESSORIES, CLOSURES, OR FITTINGS THEREFOR; PACKAGING ELEMENTS; PACKAGES
    • B65D88/00Large containers
    • B65D88/54Large containers characterised by means facilitating filling or emptying
    • B65D88/72Fluidising devices

Definitions

  • the present invention relates to a discharge apparatus for a funnel-shaped container with an outlet at its narrow end, having a number of elements made of a gas-permeable material provided within the container on its wall so as to extend towards the outlet of the container in such a manner that a channel sealed along the edges of the elements is defined between each particular element and the wall of the container, the channel being divided into separate sections by means of transverse partition walls, and gas supply conduits being provided for these sections.
  • Bridging is a frequently occurring problem in the discharge of various materials from the lower end of funnel-shaped containers, which often form the lower end of a silo but can be open at the top as well.
  • the bridging causes the discharge to be interrupted more or less temporarily.
  • DE-A-1506977 discloses discharge apparatus which comprises a container with inclined side walls and an opening in its base. Porous elements are provided in the side walls. Air is supplied to the porous elements at a pressure selected according to the distribution of material in the container, to ensure that the distribution remains even.
  • the object of the invention is to provide an inexpensive discharge apparatus for powders, which allows a controllable and uninterrupted even discharge to be achieved, even with powders which are extremely liable to bridging.
  • the present invention provides an apparatus according to the introduction, in which apparatus each gas supply conduit is provided with a throttle provided by an apertured plate selected according to the material to be discharged from the container, the plate being capable of being removed from the conduit.
  • the elements made of a gas-permeable material are preferably arranged to extend at least substantially from the outlet of the funnel-shaped container up to the inlet end of the container.
  • gas is supplied to all the channel sections from a common source.
  • the gas supply conduits provided for each channel section is throttled by means of a throttle plate the throttle opening of which is chosen so as to suit the properties of the active dry powder.
  • the gas-permeable elements are preferably made of a weldable sheet metal available on the market under the name DYNAPORE®, whereby the pores in the sheet metal are preferably directed obliquely downward and towards the outlet of the funnel-shaped container.
  • Other materials for so called fluidised conveying can be used as well.
  • the throttled supply of gas into the separate channel sections between the wall of the container and the elements of gas-permeable material provides an uninterrupted even discharge of material, also when the material level in the funnel-shaped container is descending, right down to the outlet opening.
  • Figure 1 is a longitudinal sectional view of a funnel-shaped container with the apparatus according to the invention, the container forming a bottom at the lower end of a silo.
  • Figure 2 is a cross-sectional view through the upper end of the funnel-shaped silo bottom.
  • Figure 3 is an enlarged partial sectional view of the wall of the silo bottom at an element made of a material permeable to gas.
  • Figure 4 is an enlarged longitudinal sectional view of a gas supply conduit provided with a throttle.
  • Figure 5 is an enlarged partial longitudinal sectional view of the wall of the silo bottom and an element of gas-permeable material.
  • a funnel-shaped, preferably conical container forming the bottom at the lower end of a silo is designated generally by the reference numeral 1; the silo is designated by 17.
  • the conical wall of the container 1 is designated by 2.
  • An outlet 3 is provided at the lower end of the bottom part 1.
  • a conventional pivotable valve plate (not shown in the drawing) can be provided in the outlet 3.
  • a number of elements 4 is mounted on the inside of the wall 2.
  • the elements are made of a gas-permeable material, preferable of a sheet metal available on the market under the name DYNAPORE®, consisting of a porous metal sheet about 3 mm in thickness and welded up of a close-meshed metal network. Pores 7 in the sheet, Figure 5, are preferably directed obliquely downward towards the outlet 3 of the funnel.
  • the edges of the sheet elements 4 are welded to the wall 2, so that a channel 5 is defined between each sheet element 4 and the wall 2.
  • Two such edge welds 6 are visible in Figure 3; in Figures 1 and 2, these welds are shown by means of dashes.
  • the elements 4 extend from the upper end of the bottom part 1, which can be open at the top as well, down to the outlet 3.
  • the channels 5 are divided into separate sections 9 by means of transverse partition walls 8. The sections are positioned one after another from the top towards the outlet 3.
  • a separate gas supply conduit 10 is provided for each channel section 9, the gas being mostly air or nitrogen, for instance.
  • Each supply conduit 10 comprises a throttle 11.
  • the throttle 11 can be formed by means of a throttle plate with a constant throttle opening suited for the properties of the material.
  • 12 designates a rubber hose and 13 a hose clamp. The throttle plate is replaced whenever required.
  • the supply of gas is preferably carried out from a common source the outlet conduit of which is designated with 14. 15 designates the extension of the conduit 14 along the wall of the bottom part 1, and 16 designates annular distribution conduits extending around the bottom part 1 up to each particular channel section 9.
  • Gas trickling out through the elements 4 activates the material in the bottom part 1 so that an uninterrupted even flow is obtained through the outlet 3.
  • the channels 5 are divided into the separate transverse sections 9 and the supply of gas into each section 9 is throttled, the discharge of the material takes place evenly even when the material level in the bottom part 1 is descending.
  • the throttles 11 prevent the gas from "escaping" through the uncovered element portions.
  • the combination of the throttled supply of gas and the provision of the separate channel sections also keeps the consumption of gas at a low level, which is an advantage not only economically but also for the reason that high consumption of gas involves filtering problems with the excess gas to avoid formation of dust.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Filling Or Emptying Of Bunkers, Hoppers, And Tanks (AREA)

Abstract

The invention relates to a discharge apparatus for a funnel-shaped container (1) with an outlet (3) at its narrow end. The object is to provide an even discharge of a powder material highly liable to the bridging, until the container is empty. This is achieved by positioning, on the inside of the container wall (2), elements (4) made of a gas-permeable material and extending towards the outlet (3), whereby each channel defined between the elements (4) and the container wall (2) is divided into separate transverse sections (9) each provided with throttled supply of gas. The gas penetrating through the elements (4) activates the powder so that an even flow out is achieved. Due to the throttled supply of gas, the even flow continues until the container (1) is empty.

Description

  • The present invention relates to a discharge apparatus for a funnel-shaped container with an outlet at its narrow end, having a number of elements made of a gas-permeable material provided within the container on its wall so as to extend towards the outlet of the container in such a manner that a channel sealed along the edges of the elements is defined between each particular element and the wall of the container, the channel being divided into separate sections by means of transverse partition walls, and gas supply conduits being provided for these sections.
  • Bridging is a frequently occurring problem in the discharge of various materials from the lower end of funnel-shaped containers, which often form the lower end of a silo but can be open at the top as well. The bridging causes the discharge to be interrupted more or less temporarily.
  • A great variety of solutions have been suggested to eliminated bridging. A common feature of all these prior art solutions is that while they prevent permanent bridges and permanent discharge interruptions, the discharge is uneven. The container can be emptied at a relatively accurately defined average rate over a longer period of time; the discharge, however, takes place in relatively violent thrusts alternating with periods of less discharge or no discharge at all.
  • DE-A-1506977 discloses discharge apparatus which comprises a container with inclined side walls and an opening in its base. Porous elements are provided in the side walls. Air is supplied to the porous elements at a pressure selected according to the distribution of material in the container, to ensure that the distribution remains even.
  • The object of the invention is to provide an inexpensive discharge apparatus for powders, which allows a controllable and uninterrupted even discharge to be achieved, even with powders which are extremely liable to bridging.
  • Accordingly, the present invention provides an apparatus according to the introduction, in which apparatus each gas supply conduit is provided with a throttle provided by an apertured plate selected according to the material to be discharged from the container, the plate being capable of being removed from the conduit.
  • The elements made of a gas-permeable material are preferably arranged to extend at least substantially from the outlet of the funnel-shaped container up to the inlet end of the container.
  • Preferably, gas is supplied to all the channel sections from a common source. The gas supply conduits provided for each channel section is throttled by means of a throttle plate the throttle opening of which is chosen so as to suit the properties of the active dry powder.
  • The gas-permeable elements are preferably made of a weldable sheet metal available on the market under the name DYNAPORE®, whereby the pores in the sheet metal are preferably directed obliquely downward and towards the outlet of the funnel-shaped container. Other materials for so called fluidised conveying can be used as well.
  • The throttled supply of gas into the separate channel sections between the wall of the container and the elements of gas-permeable material provides an uninterrupted even discharge of material, also when the material level in the funnel-shaped container is descending, right down to the outlet opening.
  • In the following, the invention will be described in more detail, with reference to a preferred embodiment shown in the attached drawing.
  • Figure 1 is a longitudinal sectional view of a funnel-shaped container with the apparatus according to the invention, the container forming a bottom at the lower end of a silo.
  • Figure 2 is a cross-sectional view through the upper end of the funnel-shaped silo bottom.
  • Figure 3 is an enlarged partial sectional view of the wall of the silo bottom at an element made of a material permeable to gas.
  • Figure 4 is an enlarged longitudinal sectional view of a gas supply conduit provided with a throttle.
  • Figure 5 is an enlarged partial longitudinal sectional view of the wall of the silo bottom and an element of gas-permeable material.
  • A funnel-shaped, preferably conical container forming the bottom at the lower end of a silo is designated generally by the reference numeral 1; the silo is designated by 17. The conical wall of the container 1 is designated by 2. An outlet 3 is provided at the lower end of the bottom part 1. A conventional pivotable valve plate (not shown in the drawing) can be provided in the outlet 3.
  • A number of elements 4 is mounted on the inside of the wall 2. The elements are made of a gas-permeable material, preferable of a sheet metal available on the market under the name DYNAPORE®, consisting of a porous metal sheet about 3 mm in thickness and welded up of a close-meshed metal network. Pores 7 in the sheet, Figure 5, are preferably directed obliquely downward towards the outlet 3 of the funnel.
  • The edges of the sheet elements 4 are welded to the wall 2, so that a channel 5 is defined between each sheet element 4 and the wall 2. Two such edge welds 6 are visible in Figure 3; in Figures 1 and 2, these welds are shown by means of dashes. The elements 4 extend from the upper end of the bottom part 1, which can be open at the top as well, down to the outlet 3. The channels 5 are divided into separate sections 9 by means of transverse partition walls 8. The sections are positioned one after another from the top towards the outlet 3. A separate gas supply conduit 10 is provided for each channel section 9, the gas being mostly air or nitrogen, for instance. Each supply conduit 10 comprises a throttle 11. As appears from Figure 4, the throttle 11 can be formed by means of a throttle plate with a constant throttle opening suited for the properties of the material. 12 designates a rubber hose and 13 a hose clamp. The throttle plate is replaced whenever required.
  • The supply of gas is preferably carried out from a common source the outlet conduit of which is designated with 14. 15 designates the extension of the conduit 14 along the wall of the bottom part 1, and 16 designates annular distribution conduits extending around the bottom part 1 up to each particular channel section 9.
  • Gas trickling out through the elements 4 activates the material in the bottom part 1 so that an uninterrupted even flow is obtained through the outlet 3. As the channels 5 are divided into the separate transverse sections 9 and the supply of gas into each section 9 is throttled, the discharge of the material takes place evenly even when the material level in the bottom part 1 is descending. In spite of the fact that the uppermost portions of the elements become uncovered so that the flow resistance is decreased, the throttles 11 prevent the gas from "escaping" through the uncovered element portions.
  • The combination of the throttled supply of gas and the provision of the separate channel sections also keeps the consumption of gas at a low level, which is an advantage not only economically but also for the reason that high consumption of gas involves filtering problems with the excess gas to avoid formation of dust.
  • From the technical point of view, it would be preferable to coat the entire inside of the bottom part 1 with a gas-permeable material; this, however, would be unreasonably expensive. A fully satisfactory result is achieved by coating only part of the inside the funnel wall, e.g. with four elements as shown in the drawing. The desired result is also achieved with three elements only, especially if they are slightly wider. If a greater number of elements 4 is used, the individual elements can, of course, be narrower.
  • Full-scale experiments have been performed on the apparatus with dry fibre-containing powders. Previously, a satisfactory discharge of fibre-containing materials has not been possible with methods used for the purpose. The silo used in the experiment was provided with a closing device resembling a throttle valve in the outlet of the funnel-shaped bottom part. When the closing device was opened wide open, the valve plate dug a hole in the dry powder positioned above it without that the powder began to flow out of the silo. But when the supply of gas according to the invention was initiated, the material began to flow out, and the flow continued uninterruptedly and homogeneously as long as gas was being supplied. When the supply of gas was interrupted, the flow ended. At a low material level in the silo, that is, when the silo was nearly empty, no gas flow causing dust problems occurred from the uncovered portion of the silo bottom, when the throttling according to the invention was suitably chosen in view of the properties of the material. No dust filter was required.

Claims (3)

  1. A discharge apparatus for a funnel-shaped container with an outlet at its narrow end, having a number of elements (4) made of a gas-permeable material provided within the container (1) on its wall (2) so as to extend towards the outlet (3) of the container in such a manner that a channel (5) sealed along the edges of the elements is defined between each particular element (4) and the wall (2) of the container (1), the channel (5) being divided into separate sections (9) by means of transverse partition walls (8), and gas supply conduits (10) being provided for these sections, characterised in that each gas supply conduit (10) is provided with a throttle (11) provided by an apertured plate selected according to the material to be discharged from the container, the plate being capable of being removed from the conduit.
  2. A discharge apparatus according to claim 1, in which a slit is formed in the conduit (10) for receiving the apertured plate (11), the apparatus including a sealing member (12, 13) to be positioned around the slit and adjacent portions of the conduit (10).
  3. A discharge apparatus as claimed in claim 2, in which the sealing member (12, 13) is sleeve-like.
EP19890906122 1988-05-25 1989-05-24 A discharge apparatus Expired - Lifetime EP0409904B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT89906122T ATE97380T1 (en) 1988-05-25 1989-05-24 DISCHARGE DEVICE.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI882470A FI80430C (en) 1988-05-25 1988-05-25 Output device
FI882470 1988-05-25

Publications (2)

Publication Number Publication Date
EP0409904A1 EP0409904A1 (en) 1991-01-30
EP0409904B1 true EP0409904B1 (en) 1993-11-18

Family

ID=8526517

Family Applications (1)

Application Number Title Priority Date Filing Date
EP19890906122 Expired - Lifetime EP0409904B1 (en) 1988-05-25 1989-05-24 A discharge apparatus

Country Status (6)

Country Link
EP (1) EP0409904B1 (en)
JP (1) JP2801940B2 (en)
DE (1) DE68910819T2 (en)
DK (1) DK171178B1 (en)
FI (1) FI80430C (en)
WO (1) WO1989011378A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007077294A1 (en) * 2005-12-30 2007-07-12 Lahti Precision Oy Metering valve

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI96297C (en) * 1993-06-24 1996-06-10 Raute Precision Oy Apparatus for dispensing a powdered substance from a tank
FI115518B (en) 2002-06-12 2005-05-31 Raute Prec Oy Powder drainage device
DE102008014475A1 (en) 2008-03-17 2009-11-12 Uhde Gmbh Method and device for the metered removal of a fine to coarse-grained solid or solid mixture from a storage container
DE102008024576B3 (en) * 2008-05-21 2009-10-01 Uhde Gmbh Device for discharging a solid from a container
DE102010018841A1 (en) 2010-04-29 2011-11-03 Uhde Gmbh discharge cone
US10228077B2 (en) 2017-03-15 2019-03-12 The Young Industries, Inc. Fluidizing butterfly valve, and system

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2723054A (en) 1951-10-04 1955-11-08 Nat Lead Co Feeders
DE1506977B2 (en) 1967-06-20 1973-11-22 Fa. Johannes Moeller, 2000 Hamburg Method and device for loosening the fine-grained goods stored in a silo
US3645583A (en) * 1970-04-09 1972-02-29 Calvin P Heath Apparatus and method for handling finely divided solids
US3713564A (en) * 1971-06-25 1973-01-30 Butler Manufacturing Co Method and means for facilitating the flow of granular materials
JPS5628815A (en) * 1979-08-16 1981-03-23 Toshiba Corp Method of forming photodiffusion-roughened surface
SE452875B (en) * 1984-04-26 1987-12-21 Hans E Eriksson Powdery material container with movable wall

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2007077294A1 (en) * 2005-12-30 2007-07-12 Lahti Precision Oy Metering valve

Also Published As

Publication number Publication date
DK171178B1 (en) 1996-07-15
DE68910819D1 (en) 1993-12-23
EP0409904A1 (en) 1991-01-30
FI882470A (en) 1989-11-26
JP2801940B2 (en) 1998-09-21
WO1989011378A1 (en) 1989-11-30
FI882470A0 (en) 1988-05-25
JPH03504483A (en) 1991-10-03
DK266290A (en) 1990-11-06
DK266290D0 (en) 1990-11-06
FI80430B (en) 1990-02-28
FI80430C (en) 1990-06-11
DE68910819T2 (en) 1994-03-17

Similar Documents

Publication Publication Date Title
CA2269626C (en) Pneumatically conveying powdery substances
EP0409904B1 (en) A discharge apparatus
JP2003502242A5 (en)
CA1101380A (en) Constant vacuum barge unloading system
US3955853A (en) Self-contained device for the pneumatic conveyance of incoherent solid materials with a modular takeup device and valve means
CA1169655A (en) Particulate solid storage container and transport method
CZ299946B6 (en) Method of and system for distribution of fluidizable materials
EP1041022B1 (en) Method for off-loading incoherent material from a container and apparatus for the implementation of the method.
US4878758A (en) Process for mixing bulk materials
DE2733077B2 (en) Device for ventilating and transporting suspended powdery materials from a tank
US6365858B1 (en) Device for separating metal parts
US5140935A (en) Fluidization arrangement for an electrostatic powder coating device
JPH02127317A (en) Apparatus and method for supplying resin molding material
US3357748A (en) Material feed regulator
CZ275593A3 (en) Unloading of a vehicle and a vehicle for transportation of material in to form of a powder, granules and/or rolls
CA2045638A1 (en) Feeder for particulate material
JP2562341Y2 (en) Powder filling equipment
JP2001278384A (en) Granule storage tank device
JP2002148092A (en) Measuring device of powder and granular material
US5205094A (en) Silo including a device for preventing obstruction to air flow
Scheibe et al. Feed characteristic of a rotary valve in a hopper feeder system
JPS5841200Y2 (en) Powder container discharge aid
SU1298163A1 (en) Method for pneumatic reloading of loose materials and device for effecting same
JPS60161827A (en) Quantitative takeout method of gas fluidized pulverulent body and device thereof
JPH0454971Y2 (en)

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: 19901106

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE CH DE FR GB IT LI LU NL SE

17Q First examination report despatched

Effective date: 19920623

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 FR GB IT LI LU NL SE

REF Corresponds to:

Ref document number: 97380

Country of ref document: AT

Date of ref document: 19931215

Kind code of ref document: T

ITF It: translation for a ep patent filed

Owner name: MARCHI & MITTLER S.R

REF Corresponds to:

Ref document number: 68910819

Country of ref document: DE

Date of ref document: 19931223

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: 19940531

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
EAL Se: european patent in force in sweden

Ref document number: 89906122.0

REG Reference to a national code

Ref country code: CH

Ref legal event code: PUE

Owner name: OY PARTEK AB TRANSFER- RAUTE DRY MIX OY

NLS Nl: assignments of ep-patents

Owner name: RAUTE DRY MIX OY

NLT1 Nl: modifications of names registered in virtue of documents presented to the patent office pursuant to art. 16 a, paragraph 1

Owner name: PARTEK OY AB

REG Reference to a national code

Ref country code: GB

Ref legal event code: 732E

BECH Be: change of holder

Free format text: 971015 *RAUTE DRY MIX OY

REG Reference to a national code

Ref country code: FR

Ref legal event code: TP

REG Reference to a national code

Ref country code: GB

Ref legal event code: IF02

REG Reference to a national code

Ref country code: CH

Ref legal event code: PFA

Owner name: RAUTE DRY MIX OY

Free format text: RAUTE DRY MIX OY#MESTARINKATU 10#15800 LAHTI (FI) -TRANSFER TO- RAUTE DRY MIX OY#MESTARINKATU 10#15800 LAHTI (FI)

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

Ref country code: CH

Payment date: 20080514

Year of fee payment: 20

Ref country code: DE

Payment date: 20080522

Year of fee payment: 20

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

Ref country code: AT

Payment date: 20080522

Year of fee payment: 20

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

Ref country code: BE

Payment date: 20080522

Year of fee payment: 20

Ref country code: IT

Payment date: 20080527

Year of fee payment: 20

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

Ref country code: SE

Payment date: 20080520

Year of fee payment: 20

Ref country code: NL

Payment date: 20080516

Year of fee payment: 20

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

Ref country code: GB

Payment date: 20080522

Year of fee payment: 20

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

BE20 Be: patent expired

Owner name: *RAUTE DRY MIX OY

Effective date: 20090524

REG Reference to a national code

Ref country code: GB

Ref legal event code: PE20

Expiry date: 20090523

EUG Se: european patent has lapsed
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 EXPIRATION OF PROTECTION

Effective date: 20090524

NLV7 Nl: ceased due to reaching the maximum lifetime of a patent

Effective date: 20090524

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 EXPIRATION OF PROTECTION

Effective date: 20090523

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

Ref country code: FR

Payment date: 20080430

Year of fee payment: 20