EP0548317A1 - Procede et dispositif pour le melange de composants de boissons. - Google Patents
Procede et dispositif pour le melange de composants de boissons.Info
- Publication number
- EP0548317A1 EP0548317A1 EP92914688A EP92914688A EP0548317A1 EP 0548317 A1 EP0548317 A1 EP 0548317A1 EP 92914688 A EP92914688 A EP 92914688A EP 92914688 A EP92914688 A EP 92914688A EP 0548317 A1 EP0548317 A1 EP 0548317A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- component
- measuring
- space
- syrup
- line
- 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
Links
- 238000000034 method Methods 0.000 title claims abstract description 24
- 239000006188 syrup Substances 0.000 claims abstract description 49
- 235000020357 syrup Nutrition 0.000 claims abstract description 49
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 32
- 235000013361 beverage Nutrition 0.000 claims abstract description 12
- 239000000523 sample Substances 0.000 claims description 22
- 238000011144 upstream manufacturing Methods 0.000 claims 1
- 238000005259 measurement Methods 0.000 abstract description 3
- 239000000203 mixture Substances 0.000 description 14
- 230000007704 transition Effects 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000018109 developmental process Effects 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 235000012174 carbonated soft drink Nutrition 0.000 description 1
- 239000000306 component Substances 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 230000001960 triggered effect Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/80—Forming a predetermined ratio of the substances to be mixed
- B01F35/88—Forming a predetermined ratio of the substances to be mixed by feeding the materials batchwise
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/40—Mixing liquids with liquids; Emulsifying
- B01F23/49—Mixing systems, i.e. flow charts or diagrams
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/81—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles
- B01F33/812—Combinations of similar mixers, e.g. with rotary stirring devices in two or more receptacles in two or more alternative mixing receptacles, e.g. mixing in one receptacle and dispensing from another receptacle
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2101/00—Mixing characterised by the nature of the mixed materials or by the application field
- B01F2101/06—Mixing of food ingredients
- B01F2101/14—Mixing of ingredients for non-alcoholic beverages; Dissolving sugar in water
Definitions
- the invention relates to a method and a device for mixing beverage components according to the preambles of claims 1 and 9.
- Such a method and such a device is known from DE-PS 31 32 706.
- the known device is used to mix a smaller amount of syrup (first component) with a larger amount of water (second component).
- a separate measuring room is provided for each component.
- the measuring room for water is equipped with a fill level meter, through which the water volume is metered.
- the volume of the syrup measuring area corresponds to the volume of syrup required for a batch and is completely filled with every mixing process.
- the measuring room for syrup is arranged below the measuring room for water and connected to it via a pipe.
- the measuring chamber with a certain volume for the syrup is combined with the measuring chamber arranged above it with a filling height meter for the water to form a cross-sectional enlargement which promotes mixing in the transition area to a receiving chamber for a complete mixture quantity.
- a fixed level probe is arranged in the upper area of the measuring space for the syrup Measuring room defined.
- syrup is first introduced into the lower measuring room until the fixed level probe is reached.
- water is also introduced into the lower measuring chamber, mixing with the syrup until a certain amount of mixture, registered by the level gauge, is reached. This amount of mixture is then discharged through a pipeline connected to the underside of the lower measuring chamber and mixed again into a collecting chamber.
- the invention has for its object to provide a method and a structurally simple device for batch-wise mixing of beverage components, with which even subsets of the first component, the volume of which is smaller than the volume of the measuring space, can be processed efficiently with a consistently high mixing accuracy.
- the quantity contained in the storage space is independent of the size Remaining amount always an exact adherence to the desired mixing ratio possible. Even small residual amounts of the syrup or the like, which previously could not be processed economically, can therefore be reliably processed without sacrificing beverage quality.
- the second component can be dosed by the dosing device operating in normal operation. According to a development of the invention contained in the subclaims, however, the measurement of the second component takes place at the same location or with the same device with which the first component is measured during the so-called residual quantity metering. This results in a particularly precise and efficient way of working.
- FIG. 1 shows the schematic side view of a device for mixing beverage components. This is integrated into a system for producing a carbonated soft drink, which is only partially shown.
- the device shown is set up for mixing a first component in the form of syrup S and a second component in the form of deaerated water W and has a container-shaped metering and mixing unit 16.
- a lower measuring chamber 2 with a circular cross-section is set up for the syrup, the volume of which is limited by a fixed level probe 23 at the level of the dash-dotted line.
- a filling height meter 18 is arranged in the receiving space 17 and registers the height of the mixture G consisting of syrup and water in the metering and mixing unit 16.
- a feed line 12 for the vented water and two intermediate shut-off valves 26, 27 with a different cross-section open an intermediate line 3 for the syrup via two shut-off valves 24, 25 with different cross-sections.
- the intermediate line 3 is connected to the bottom of a flow container 28 with a storage space 1 for the syrup, which is at a higher level than the measuring space 2.
- the flow container 28 is equipped with a lower level probe 14 and an upper level probe 22 and is via a syrup line 21 supplied with a control valve 29.
- the flow tank 28 is connected via a line 20 to a CO 2 collecting line 37, as is the metering and mixing unit 16 via a line 19.
- the measuring chamber 2 has, below its level sensor 23 determining the volume, a further level sensor 30 for controlling the filling speed.
- a drain 5 with a shut-off valve 31 is connected to its lowest point, which leads into a tank 32 a collecting space 4 opens out for the mixture.
- a further line 33 leads from the tank 32 with a pump 34 to a saturation tank (not shown), in which the mixture is impregnated with carbon dioxide and to which the CO line 37 is connected.
- a few further metering and mixing units are connected to the tank 32 with the collecting space 4 for the mixture, which match the structure of the metering and mixing unit 16 described so far. In this way, the various dosing and mixing units can be filled and emptied alternately and it is possible to feed the collecting space 4 evenly.
- a secondary line 6 is connected, which opens into the measuring space 2 of the metering and mixing unit 16.
- a first shut-off valve 7, a pump 10, an empty sensor 11, an inductive flow meter 9 and a second shut-off valve 8 are connected in sequence, the latter and the flow meter 9 being located near the junction parts of the secondary line 6 into the measuring chamber 2.
- the feed line 12 for deaerated water is connected to the secondary line 6 via a further shut-off valve 13.
- the empty signal probe 11, the flow meter 9 and the lower fill level probe 14 in the flow tank 28 are connected to the input side of a control device 15 via signal lines indicated by dash-dotted lines.
- the level probe 14 is arranged such that it has a signal generated when the remaining amount of syrup in the storage room 1 is smaller than the volume of the measuring room 2 to the upper level probe 23.
- the empty sensor 11 is designed such that it generates a signal when the secondary line 6 is empty at this point, so neither syrup still contains water.
- the three shut-off valves 7, 8, 13 and the pump 10 are connected to the output side of the control device 15 via control lines indicated by dashed lines.
- the control device 15 has an actuator 35 with which the mixing ratio between the two components can be set.
- the storage space 1 in the flow container 28 is kept largely filled with the aid of the upper level probe 22 and the control valve 29 via the syrup line 21, which leads to a storage tank (not shown).
- the amount of syrup in the storage room 1 is then large enough to fill the measuring room 2 several times with syrup.
- the mixing of the two components S and W takes place without the cooperation of the control device 15 - with the shut-off valves 7, 8, 13 and the pump 10 switched off - according to the following procedure:
- the shut-off valve 31 when the shut-off valve 31 is closed, the syrup is introduced from the supply tank 28 via the intermediate line 3 and the open shut-off valve 26 with a larger cross-section at high speed into the measuring chamber 2 until the lower fill level probe 30 is reached. Then the valve 26 is closed again and the previously closed shut-off valve 27 opened with a smaller cross section. The syrup now flows with smaller Speed into the measuring room 2 until it reaches the upper level probe 23. The shut-off valve 27 is then also closed. The measuring room 2 is now completely filled with syrup up to its predetermined volume.
- the shut-off valve 24, which has been closed until now, is opened with a larger cross section, so that deaerated water flows into the measuring chamber 2 at high speed via a pump (not shown) and the feed line 12.
- the water mixes with the syrup and the mixture rises in the receiving space 17 up to a certain fill level, registered by the fill level meter 18.
- the shut-off valve 24 is closed again and the shut-off valve 25 with a smaller cross section, which has been closed until now, is opened.
- the water is introduced into the measuring space 2 at a low speed, namely until a predetermined fill level of mixture in the receiving space 17 is reached, which in turn is registered by the fill-level meter 18.
- the control of the water supply can of course also be taken over by several fixed fill level probes.
- the predetermined fill level in the receiving space 17 which is dependent on the desired mixing ratio between syrup and water, is reached, the metering of syrup and water has ended and the two components have already been mixed for the first time.
- the complete mixture batch is now introduced via the discharge line 5 into the collecting space 4 of the tank 32 and thereby further mixed.
- the resulting mixture in the collecting space 4 is then transported via the line 33 and the pump 34 to the impregnation container, not shown, where it is carbonated and is then ready for filling.
- the fill level in the flow container 28 gradually drops, at some point to below the lower fill level probe
- the remaining amount of syrup in the storage room 1 is now no longer sufficient for a complete filling of the measuring room 2.
- the level probe 14 emits a corresponding signal and activates the control device
- shut-off valves 7 and 8 are opened; the pump 10 is switched on and the flow meter 9 is activated; the shut-off valve 13 initially remains closed. Then the remaining or partial amount of the syrup present in the storage room 1 and in the intermediate line 3 is almost completely fed into the measuring room 2 via the secondary line 6 initiated until the secondary line 6 has run empty as far as the empty signal probe 11 and this emits a control signal. Then the two valves 7 and 8, or at least the valve 7, are closed and the amount of syrup registered by the flow meter 9 is displayed and reported to the control device 15. This calculates the required amount of water from the measured amount of syrup and the set mixing ratio.
- This flow rate is now given to the flow meter 9 and water is introduced into the measuring chamber 2 via the secondary line 6 by opening the valves 13 and possibly 8 water from the supply line 12.
- this immediately causes the shut-off valves 8 and 13 to close and the pump 10 to be switched off.
- This partial batch is then introduced into the collecting space 4 in the usual manner by opening the shut-off valve 31 via the discharge line 5.
- the remaining amount of water in the secondary line 6 can be drained by opening a drain tap 36 between the shut-off valve 7 and the pump 10.
- the above-described method can also be carried out if there is sufficient syrup for a complete batch, for other reasons, for example because only a certain number of bottles have to be filled, but only a partial batch is to be mixed. In this case, the change is made manually and not automatically the level probe 14. With the aid of the flow meter 9, a simple, exact “calibration" of the level probes 23, 30 and the level gauge 18 is also possible.
- the implementation of the method according to the invention was described in connection with a device in which the measuring space for the syrup is connected to the measuring space for the water or for the mixture arranged above it via a transition region with an increasing cross-section.
- a device in which these two measuring rooms are connected via a line with a shut-off valve there are two options: If the shut-off valve is open during dosing, the process proceeds in the manner already described, since then the mixture from the lower one Measuring room for the syrup can climb into the upper measuring room. If, on the other hand, the shut-off valve is closed, the water after the partial filling of the lower measuring space with syrup into the upper measuring space for the water is measured separately, e.g. by the already existing level meter for normal operation or by the flow meter for the syrup. For this purpose, another line with a shut-off valve is connected behind the flow meter to the secondary line, which opens directly into the upper measuring chamber for the water.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Devices For Dispensing Beverages (AREA)
- Apparatus For Making Beverages (AREA)
Abstract
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE4123047A DE4123047A1 (de) | 1991-07-12 | 1991-07-12 | Verfahren und vorrichtung zum mischen von getraenkekomponenten |
DE4123047 | 1991-07-12 | ||
PCT/EP1992/001540 WO1993000988A1 (fr) | 1991-07-12 | 1992-07-08 | Procede et dispositif pour le melange de composants de boissons |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0548317A1 true EP0548317A1 (fr) | 1993-06-30 |
EP0548317B1 EP0548317B1 (fr) | 1996-01-10 |
Family
ID=6435959
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP92914688A Expired - Lifetime EP0548317B1 (fr) | 1991-07-12 | 1992-07-08 | Procede et dispositif pour le melange de composants de boissons |
Country Status (6)
Country | Link |
---|---|
US (1) | US5308160A (fr) |
EP (1) | EP0548317B1 (fr) |
JP (1) | JP2637286B2 (fr) |
DE (2) | DE4123047A1 (fr) |
ES (1) | ES2082482T3 (fr) |
WO (1) | WO1993000988A1 (fr) |
Families Citing this family (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2555250B2 (ja) * | 1992-09-18 | 1996-11-20 | 株式会社中村金属工業所 | 糖度調整用連続混合装置 |
US5572923A (en) * | 1995-06-26 | 1996-11-12 | Kuboyama; Nobuyoshi | Health beverage that an extracted ingredient from plant, animal or mineral is major ingredient, and manufacturing method and apparatus therefor |
WO1998049391A1 (fr) * | 1997-04-30 | 1998-11-05 | Kvaerner Pulping Ab | Systeme d'evacuation d'une cuve sous pression destinee au blanchiment de pate a papier |
US7980753B2 (en) | 1998-04-16 | 2011-07-19 | Air Liquide Electronics U.S. Lp | Systems and methods for managing fluids in a processing environment using a liquid ring pump and reclamation system |
US20070119816A1 (en) * | 1998-04-16 | 2007-05-31 | Urquhart Karl J | Systems and methods for reclaiming process fluids in a processing environment |
US6247838B1 (en) * | 1998-11-24 | 2001-06-19 | The Boc Group, Inc. | Method for producing a liquid mixture having a predetermined concentration of a specified component |
US6293430B1 (en) * | 1999-09-25 | 2001-09-25 | Odell Kent Haselden, Jr. | Apparatus and method for recovering beverage syrup |
FR2831835A1 (fr) * | 2001-11-07 | 2003-05-09 | Jean Pierre Loubes | Appareil pour le melange homogene de liquides |
JP4790995B2 (ja) * | 2004-03-19 | 2011-10-12 | 株式会社テクノメイト | スラリー希釈装置 |
US7766538B2 (en) * | 2005-09-22 | 2010-08-03 | Assembled Products Corporation | System for blending liquids in selected ratios |
WO2009069090A2 (fr) | 2007-11-27 | 2009-06-04 | L'air Liquide-Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Fonction de récupération améliorée pour systèmes de traitement de semi-conducteurs |
EP2272384A1 (fr) * | 2009-07-08 | 2011-01-12 | INDAG Gesellschaft für Industriebedarf mbH & Co. Betriebs KG | Procédé et dispositif destinés à la fabrication de boissons |
DE102010029125A1 (de) * | 2010-05-19 | 2011-11-24 | Krones Ag | Vorrichtung und Verfahren zum Ausmischen von Getränken |
DE102010025690A1 (de) | 2010-06-30 | 2012-01-05 | Khs Gmbh | Verfahren und Anlage zur Herstellung von Fluidgemischen, z.B. Getränken |
DE102012215530A1 (de) | 2012-08-31 | 2014-03-06 | Krones Ag | Misch-Regelventil |
US20160296902A1 (en) | 2016-06-17 | 2016-10-13 | Air Liquide Electronics U.S. Lp | Deterministic feedback blender |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB781818A (en) * | 1955-07-25 | 1957-08-28 | Karel Mattheus Burlage | Mixing apparatus for supply of a certain amount of liquid mixture |
DE2758096C2 (de) * | 1977-12-24 | 1984-05-24 | Behr, Hans, 7000 Stuttgart | Verfahren und Vorrichtung zum automatischen dynamischen Dosieren mindestens einer flüssigen Komponente einer Mischflüssigkeit |
US4323902A (en) * | 1980-10-03 | 1982-04-06 | General Motors Corporation | Power antenna with resilient mounting means |
DE3132706C2 (de) * | 1981-08-19 | 1991-03-07 | Ortmann & Herbst Gmbh, 2000 Hamburg | Vorrichtung zum Dosieren, Entlüften und Karbonisieren von Mehrkomponentengetränken |
US4691850A (en) * | 1984-08-09 | 1987-09-08 | Kirschmann John D | Chemical dispensing system |
US4784495A (en) * | 1987-02-06 | 1988-11-15 | Gambro Ab | System for preparing a fluid intended for a medical procedure by mixing at least one concentrate in powder form with water |
JPH01270931A (ja) * | 1988-04-22 | 1989-10-30 | Kurin Engine Kenkyusho:Kk | 薬品希釈混合装置 |
-
1991
- 1991-07-12 DE DE4123047A patent/DE4123047A1/de not_active Withdrawn
-
1992
- 1992-07-08 EP EP92914688A patent/EP0548317B1/fr not_active Expired - Lifetime
- 1992-07-08 DE DE59205017T patent/DE59205017D1/de not_active Expired - Fee Related
- 1992-07-08 US US07/969,246 patent/US5308160A/en not_active Expired - Lifetime
- 1992-07-08 ES ES92914688T patent/ES2082482T3/es not_active Expired - Lifetime
- 1992-07-08 JP JP5501972A patent/JP2637286B2/ja not_active Expired - Fee Related
- 1992-07-08 WO PCT/EP1992/001540 patent/WO1993000988A1/fr active IP Right Grant
Non-Patent Citations (1)
Title |
---|
See references of WO9300988A1 * |
Also Published As
Publication number | Publication date |
---|---|
JPH06500502A (ja) | 1994-01-20 |
US5308160A (en) | 1994-05-03 |
ES2082482T3 (es) | 1996-03-16 |
WO1993000988A1 (fr) | 1993-01-21 |
JP2637286B2 (ja) | 1997-08-06 |
DE4123047A1 (de) | 1993-01-14 |
DE59205017D1 (de) | 1996-02-22 |
EP0548317B1 (fr) | 1996-01-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0548317B1 (fr) | Procede et dispositif pour le melange de composants de boissons | |
EP0105842B1 (fr) | Procédé et appareil pour la préparation de mélanges liquides | |
DE4114673C1 (fr) | ||
DE2042927B2 (de) | Verfahren und Vorrichtung zur Prüfung von ungereinigtem Rohwasser bei der Aufbereitung | |
EP0432673B1 (fr) | Dispositif mobile pour produire des mélanges actifs sur base de l'eau | |
DD284578A5 (de) | Einrichtung zum aufbereiten und zufuehren von pumpfaehigen viehfuttermischungen | |
DE603664C (de) | Vorrichtung zur Herstellung von Loesungen gleichmaessiger Konzentration unmittelbar aus Salzen | |
EP1397662A2 (fr) | Procede et dispositif de prelevement d'un echantillon dans une charge fluidique | |
EP0123041B1 (fr) | Procédé et dispositif pour alimenter un mélangeur | |
DE2642788C2 (de) | Vorrichtung zur diskontinuierlichen Herstellung von Lösungen definierter Konzentration | |
DE4237933A1 (de) | Verfahren und Vorrichtung zum Herstellen von Getränken aus mehreren flüssigen Komponenten | |
DE4140358C2 (de) | Verfahren und Vorrichtung zur Erzeugung exakter Mischungsverhältnisse insbesondere bei der Verdünnung von Belebtschlamm mit Klarwasser | |
DE4118961C2 (de) | Verfahren und Vorrichtung zum Zuführen von Zusatzflüssigkeit, insbesondere von Zusätzen zu einer fotografischen Behandlungsflüssigkeit | |
DE4138477A1 (de) | Dosierpumpen-einstellung | |
DE4130413C2 (de) | Anlage zum Mischen und/oder Homogenisieren flüssiger Komponenten | |
AT396377B (de) | Verfahren und vorrichtung zum befuellen des verbraucherbehaelters eines mit einer feuchtsalzstreueinrichtung versehenen winterdienststreufahrzeuges | |
DE4343717A1 (de) | Verfahren und Vorrichtung zum Entnehmen einer für ein Milchvolumen repräsentativen Milchprobe | |
DE2852372A1 (de) | Verfahren und vorrichtung zum automatischen dosieren von fluessigkeiten, die einer zu behandelnden fluessigkeit zugesetzt werden | |
DE3202314A1 (de) | Vorrichtung zum zumischen von fluessigen chemikalien, insbesondere desinfektions- oder reinigungsmittel, zu fluessigkeiten, vorzugsweise wasser | |
DE2723623A1 (de) | Vorrichtung zum zuteilen von fraktionen | |
DE19625651C2 (de) | Vorrichtung zum Mischen von wenigstens zwei Flüssigkeiten | |
DE4038770A1 (de) | Verfahren und vorrichtung zum herstellen von getraenken | |
DE1962740A1 (de) | Vorrichtung zur Herstellung von schaumigen Massen,insbesondere Schlagsahne | |
DE9204973U1 (de) | Ansetzstation | |
DE1251278B (fr) |
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: 19930105 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): DE ES FR GB IT |
|
17Q | First examination report despatched |
Effective date: 19940711 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): DE ES FR GB IT |
|
ET | Fr: translation filed | ||
ITF | It: translation for a ep patent filed |
Owner name: PATRITO BREVETTI |
|
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) |
Effective date: 19960111 |
|
REF | Corresponds to: |
Ref document number: 59205017 Country of ref document: DE Date of ref document: 19960222 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2082482 Country of ref document: ES Kind code of ref document: T3 |
|
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: ES Payment date: 20050704 Year of fee payment: 14 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FD2A Effective date: 20060710 |
|
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: 20060710 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20080717 Year of fee payment: 17 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: IT Payment date: 20080731 Year of fee payment: 17 Ref country code: FR Payment date: 20080718 Year of fee payment: 17 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 20080709 Year of fee payment: 17 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20090708 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST Effective date: 20100331 |
|
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: 20090731 |
|
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: 20090708 |
|
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: 20100202 |
|
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: 20090708 |