EP1379822B1 - Getränkekühlvorrichtung - Google Patents

Getränkekühlvorrichtung Download PDF

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Publication number
EP1379822B1
EP1379822B1 EP02732612A EP02732612A EP1379822B1 EP 1379822 B1 EP1379822 B1 EP 1379822B1 EP 02732612 A EP02732612 A EP 02732612A EP 02732612 A EP02732612 A EP 02732612A EP 1379822 B1 EP1379822 B1 EP 1379822B1
Authority
EP
European Patent Office
Prior art keywords
evaporator
container
water
cooler according
leg
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
EP02732612A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP1379822A1 (de
Inventor
Martin Behle
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.)
Hartek Beverage Handling GmbH
Original Assignee
Hartek Beverage Handling GmbH
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 Hartek Beverage Handling GmbH filed Critical Hartek Beverage Handling GmbH
Publication of EP1379822A1 publication Critical patent/EP1379822A1/de
Application granted granted Critical
Publication of EP1379822B1 publication Critical patent/EP1379822B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/02—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled
    • F28D7/024—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled the conduits of only one medium being helically coiled tubes, the coils having a cylindrical configuration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
    • B01F27/91—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with propellers
    • 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
    • B01F35/90—Heating or cooling systems
    • B01F35/93—Heating or cooling systems arranged inside the receptacle
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67D—DISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
    • B67D1/00—Apparatus or devices for dispensing beverages on draught
    • B67D1/08—Details
    • B67D1/0857—Cooling arrangements
    • B67D1/0858—Cooling arrangements using compression systems
    • B67D1/0861—Cooling arrangements using compression systems the evaporator acting through an intermediate heat transfer means
    • B67D1/0864—Cooling arrangements using compression systems the evaporator acting through an intermediate heat transfer means in the form of a cooling bath
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
    • F25D31/00—Other cooling or freezing apparatus
    • F25D31/002—Liquid coolers, e.g. beverage cooler
    • F25D31/003—Liquid coolers, e.g. beverage cooler with immersed cooling element
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/06—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by affecting the pattern of flow of the heat-exchange media
    • 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
    • B01F35/90—Heating or cooling systems
    • B01F2035/98—Cooling
    • 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05—Stirrers
    • B01F27/11—Stirrers characterised by the configuration of the stirrers
    • B01F27/15—Stirrers with tubes for guiding the material

Definitions

  • the invention relates to a device for cooling drinks, according to the The preamble of claim 1, known from US-A-5,368,198.
  • Beverage cooling devices are in the art, for example, as so-called Beverage flow cooler or so-called Kreislaufkarbonatoren known, for example for Cooling of beer and soft drinks.
  • Known beverage cooling devices therefore have a container 20 which is filled with water is filled, the so-called water bath 12.
  • evaporator lines 14 of a refrigeration cycle arranged such that it has at least one evaporator surface 16th form, for example by the evaporator lines 14 in the form of evaporator coils or evaporator spirals are arranged side by side or one above the other.
  • the evaporator lines 14 while one or more Evaporator surfaces 16 form.
  • the evaporator lines absorb heat from the water bath 12.
  • the evaporator surface 16 may optionally be formed by the surface of a so-called ice bank 30, such as will be further described below.
  • beverage lines are for reasons of clarity in the attached figures not shown. They can be in the container in any suitable way 20, typically occupying substantially the entire space of the water bath Take advantage of 12 and center around an agitator 18 and / or near a Ice bank 30 may be arranged. The guided in the beverage lines drink gives Heat to the water bath, which cools the drink.
  • the associated Karbonatortank also be arranged in the water bath 12 (in the Figures also not shown).
  • a stirrer 18 which is a water flow S in the water bath 12 causes.
  • Figure 1 is an exemplary, temporally and spatially averaged course of the induced by the agitator 18 water flow S shown.
  • a rotation (arrow D) of the agitator 18, for example about a central axis of the Container 20 the water then flows in the middle of the container 20 initially axially after below, i. normal to the container bottom 22.
  • the flow is then deflected radially outward.
  • evaporator surfaces 16 takes place then a deflection of the flow upwards.
  • any other suitable Arrangement of the agitator 18 in the container 20 with a correspondingly different flow pattern conceivable, for example, an off-center arrangement of the agitator 18, in the the course of flow is in principle equal to the course described above.
  • thermodynamic point of view and to effect cooling of the subject Drinks serves the water of the water bath 12 both as energy storage and as Transport medium to the heat from the beverage lines to the evaporator lines 14th transferred to.
  • energy storage the water through the formation of an ice layer 30th used, which forms around the evaporator tubes 14 around.
  • ice bank whose surface corresponds to the evaporator surface 16.
  • the by the Phase transition stored enthalpy of enthalpy of water serves the short-term Dekkung of power peaks and thus reduces the performance of the refrigeration cycle process.
  • an evaporator 14, 16 but also operated without ice layer 30 are, i. the beverage cooler operates in such a case without ice bank.
  • the water is used by means of the agitator 18 in the water bath 12 induced flow S, as described above.
  • the water flow S has it to the goal, on the one hand, the heat transfer from the evaporator 14, 16 and the ice layer 30 to Water as well as from the water to the beverage lines to improve.
  • the transport of locally heated water into colder areas of the Wasserbads 12 are reinforced.
  • water as energy storage and transport medium
  • this term is representative of all other suitable media or fluids
  • the comparable Properties and functions have the same and with respect to the invention Unfold effects and provide comparable results.
  • the effects described have the consequence that the area at which the heated water to the ice layer can give off energy, is reduced in size. This will heat transfer between water bath and evaporator, but also between water bath and beverage lines, deteriorates, resulting in a loss of performance and overall reduced efficiency of Beverage cooling device is conditional. Furthermore, it may be due to the leaching A and reducing the thickness of the ice bank in the lower part of the water bath to one earlier destabilization of the ice bank, which can be a reduced peak load capacity can result. Due to a lack of rinsing the ice bank in the upper Water bath area, which in turn by the above described detachment of the flow of the ice bank is conditional, it can also cause an increased tendency to freeze come the upper beverage lines.
  • the invention is therefore based on the object, the disadvantages of the prior Technology to prevent and especially the leaching of the ice bank with the so to prevent associated disadvantages.
  • the beverage cooling device in particular a device for directing the flow of water in such a way that the water also at the in the substantially entire evaporator surface along and substantially parallel to this flows.
  • the flow dividing device has two legs, which have a substantially circular arc Intermediate piece are connected to each other, the radius of curvature is so ge noirlt that Taylor-Goertler longitudinal vortex be induced in the water flow.
  • the beverage cooling device flow guide the water flow at least partially forced so that the water in the area of the evaporator surfaces as far as possible substantially parallel to these flows, this flow along substantially the entire evaporator surface he follows. If the evaporator with an ice layer (ice bank) is operated, the runs Flow thus substantially parallel to the Eisbankober II and substantially over the entire height or length of the ice bank in the container.
  • ice bank ice bank
  • the flow guide substantially arranged on the container bottom and has a shape that the flow of water in Area of the lower end of the evaporator surfaces in one direction substantially parallel deflects to the evaporator surfaces. It is basically irrelevant whether the container walls and / or in the area of these walls or inside the container under a Distance to the container walls arranged evaporator surfaces vertically or under a Angles are arranged to the container bottom. Likewise, the shape, the course and the Arrangement of the container bottom in principle irrelevant. Evaporator surfaces and / or Container walls and / or container bottom can therefore basically under any Be arranged angle to each other.
  • the evaporator surfaces are in substantially perpendicular to the substantially planar, horizontally extending container bottom arranged, wherein the Strömungsleitvorides the water flow in this case an angle of about 90 ° deflects.
  • the flow guide is in the Form formed at least one frame profile or baffle, in the water on is mounted to the container bottom and / or in the vicinity thereof.
  • the baffle or the frame has a substantially L-shaped cross section, wherein a leg of the L-shaped sheet in is aligned substantially parallel to the evaporator surface, and wherein the other leg of the L-shaped sheet substantially parallel to the container bottom, preferably horizontally, is aligned.
  • the flow guiding device has a Frame profile, which is arranged radially inside the evaporator surfaces, wherein the in substantially aligned parallel to the evaporator surfaces leg the lower end of the Evaporator surfaces slightly overlapped.
  • the frame profile can rest on the container bottom.
  • the leg of the container aligned substantially parallel to the container bottom Frame profile on the container bottom.
  • the flow guide device in the form of a shallow pan closed bottom, which in turn is mounted on the container bottom.
  • one or more projections or embossments may be formed in the container bottom or the bottom of the tub be provided, which have a corresponding effect.
  • the evaporator surfaces at intervals to the Container bottom and / or the container walls may be arranged. This is located radially inside the evaporator surfaces arranged frame profile not on the container bottom but is arranged above this increased so that in turn substantially parallel to the evaporator surfaces aligned legs the lower end of the evaporator surfaces slightly overlapped.
  • the flow guiding device as a whole is designed and arranged in such a way that the water flow in the region of the lower end of the evaporator surfaces divided in such a way is that a water flow both radially inside and radially outside of the evaporator surfaces he follows.
  • the fluidic advantages of the frame profile or baffle Thus, not only on one side but on both sides of the ice bank, i. the radial pointing inward as well as the radially outward facing side of the ice bank, used, by dividing the water stream impinging perpendicularly on the inner surface of the ice bank, and then both behind (outside) and in front of (inside) the ice bank along the surfaces of the Ice bank is headed.
  • the heat transfer surface of the ice bank or the Evaporator approximately doubled, so that by these measures a further improved Heat transfer between water and ice bank / evaporator is effected, bringing a further increased performance and improved efficiency of the beverage cooler be achieved.
  • the Flow guiding device In the latter, second application, in which the evaporator surfaces under Distances to the container bottom and / or the container walls are arranged, the Flow guiding device have a second frame profile, below and / or at least partially disposed radially outside the evaporator surfaces.
  • This frame profile can in turn rest on the container bottom, in which case in particular the im substantially parallel to the container bottom aligned leg of the frame profile the container bottom rests.
  • a flat Tub with closed bottom can be used instead of the second frame profile.
  • the second frame be connected to the first frame to a single unit, so that the Flow guiding device used as a component in the container of the beverage cooling device can be.
  • the beverage cooler first has the features described above with respect to FIG. 1 to which reference is made.
  • FIG. 3 shows a beverage cooling device, that of the beverage cooling device shown in FIG corresponds, wherein the same features with the same reference numerals are.
  • the beverage cooling device in a first embodiment now However, a flow guide 40, which is arranged on the container bottom 22.
  • the Flow guiding device is in particular a Strömungsleitrahmen or baffle 40 a, the in perspective in Figure 5 and in cross-section in various embodiments in FIG 6 is shown.
  • this baffle frame 40a Decisive for the function of this baffle frame 40a is on the one hand its position relative to the lowermost evaporator tube 14a in the ice bank 30 or to the lowest layer of evaporator tubes 14, if these, for example, on the walls 24 of the container 20th circulate.
  • decisive for the function of the baffle frame 40a are the Shape and dimensions of the frame profile. Basically, the shape of the profile must be in the lead substantially rectangular deflection of the water flow (see Figures 3, 5 and 6), assuming that the main flow before the deflection parallel to the Container bottom 22 extends, as described above with respect to Figure 1.
  • the rectangular deflection of the water flow S causes the Water after the deflection substantially to the entire evaporator or Eisbank components 16 along and substantially parallel to this flows.
  • FIG. 6 (A) represents the simplest shaping of the frame 40 a, which the above requirements only insufficiently met.
  • shapes should be appropriate Figures 6 (B) or (C) are selected.
  • the upper leg 42 passes over an essentially arcuate intermediate piece in the lower leg 44 via.
  • the radius R decisively influences the Quality of the diversion, and he is preferably to choose as large as possible.
  • the upper leg 42 passes over an oblique intermediate piece in the lower leg 44, wherein the slope at an angle ⁇ opposite the container bottom 22 and the lower leg 44 is inclined.
  • the angle ⁇ should preferably be approximately equal to 45 °, and the slope should be as long as possible.
  • the angle ⁇ should preferably be approximately equal to 45 °, and the slope should be as long as possible.
  • Taylor-Goertler longitudinal vortices in the flow be induced.
  • Such longitudinal vortices may be at a superposition of a wall boundary layer arise with centrifugal forces, as in the present case in the overflow of the baffle given is.
  • Such longitudinal vortices can in particular have a positive effect on the Have heat transfer.
  • the upper leg 42 of the frame 40a may in turn be aligned parallel to the evaporator / ice bank surface 16, i. he forms the same angle with the lower leg 44 of the frame 40a as between Evaporator / Eisbank constitutional 16 and container bottom 22 is formed.
  • the length h of the upper leg 42 preferably so be selected that the leg 42 preferably 25% to 50% of the diameter of the lowest evaporator tube 14a of the evaporator surface 16 and the lowest layer of Evaporator tubes 14 covered.
  • the length h thus depends on the arrangement of the evaporator in the container 20 and in particular from the height of the lowest evaporator tube 14a of the evaporator above the container bottom 22, wherein as a reference point of the position of the Evaporator in the container typically the point with the greatest distance to the Container bottom is selected.
  • the length t of the lower leg 44 is preferably about 0.25 to 0.5 times the length h of the upper leg 42.
  • the angle ⁇ between the legs 42 and 44 of the Strömungsleitrahmens 40 preferably 90 °, so that a rectangular, to the Evaporator / Eisbank surface 16 parallel deflection of the flow is achieved. If the angle ⁇ is chosen to be greater than 90 °, the leaching effects occur in the ice bank as explained above with reference to FIG. As a result, the inventive Task can not be sufficiently solved, and the effectiveness of the flow guide would be lifted at least in part. If the angle ⁇ is less than 90 ° is chosen, the object of the invention is also not sufficiently solved since the water flow immediately after the deflection of the evaporator / Eisbank vom 16 would replace and remove them. This would be the heat transfer between Water and evaporator in turn deteriorates, bringing the performance and efficiency the beverage cooler would in turn be reduced.
  • the minimum distance of the Strömungsleitrahmens 40 from the evaporator coil results from the minimum distance X between evaporator tubes 14 and the (not shown) beverage-carrying pipes.
  • a typical guideline should be 0.5 to 0.7 times for this distance X can be selected.
  • the flow guide should also be a rectangular Have plan, as shown for the Strömungsleitrahmen 40 by way of example in Figure 5.
  • the leadership is in the corner regions of the container Water flow ensured. Due to the preferably substantially angular design of the Frame and the bending radii of the evaporator tubes in the corners of the container it comes to an increased leaching in the corner areas of the ice bank. However, this one has the Advantage that the areas most vulnerable to freezing be better protected.
  • the container and flow guide frame may be any other suitable one Have a plan, for example, a substantially circular outline.
  • the shape and the dimensions of the Strömungsleitrahmens can apply essentially analogous to the, what has been described above with reference to FIGS. 6 (A) to (C).
  • the flow guiding device formed by one or more projections 50 in the bottom 22 of the container 20, as shown by way of example in Figure 4.
  • the projection 50 in the one Container interior projecting imprint, groove or groove in the container bottom.
  • the projection must again have a leg which is substantially parallel to the Evaporator / Eisbank surface 16 is aligned so that the water flow again in such a way is deflected, that the water in turn substantially parallel to the Evaporator / Eisbank components and preferably flows substantially along the entire surface.
  • the radially inner limb of the embossing 50 effects the Redirecting the flow of water upwards.
  • the projection or embossing overlaps 50 the lower end of the evaporator / Eisbank surface again slightly, as it is in principle above in Reference to the upper, substantially perpendicular leg 42 of the L-shaped Frame profile 40a has been described.
  • the embossing or the projection is 50 radially disposed at the outermost position of the container bottom 22, ie in the lower, outer corner of the container, so that they are just below the evaporator surface or the Ice bank 30 is located.
  • the radially inner leg of the embossing 50 can to a certain extent form the extension of the evaporator / Eisbank materials 16 down, with a deflection the water flow S up again through this parallel to the Evaporator / Eisbank materials 16 aligned legs is effected.
  • Strömungsleitrahmens 40 has opposite projections or embossments 50th in the container bottom the advantage that the operation of the beverage cooling device more individual and more flexible can be done by putting in the same cooling device as needed different sized Strömungsleitrahmen 40 can be used.
  • embossments 50 rigidly and integrally connected to the container 20.
  • the Production of Strömungsleitrahmens regardless of the beverage cooling container, manufacturing technology easier than the production of the embossments or protrusions in the container bottom. In the case of circulating in the container evaporator tubes or coils must also the embossing in a corresponding manner continuously circulate on the container bottom, which manufacturing technology can also be problematic.
  • the beverage cooling device according to the invention are the evaporator / Eisbank lake in essentially arranged on the container walls, and they extend substantially to the Container bottom.
  • the radially arranged within the evaporator surfaces frame profile can In this case, rest on the bottom of the container.
  • the evaporator / ice bank surfaces 16 are spaced from the container bottom 22 and the container walls 24 are arranged.
  • a controlled water flow S on both sides of the ice bank 30 achieved by the substantially parallel to the Container bottom 22 and substantially perpendicular to the ice bank 30 and the inner evaporator / Eisbank requirements 16 to be flowed water flow S in the region of the lower end of the Evaporator / Eisbank requirements 16 is divided so that a part of the water flow S along the radially inwardly facing evaporator surface 16, so to speak, inside the ice bank 30 is guided upward along this evaporator / ice bank surface 16 while the other part of the water flow S between the container wall 24 and the radial outwardly facing evaporator surface 16, so to speak outside behind the ice bank 30th along this evaporator / Eisbank requirements 16 is guided upward.
  • the container wall 24 forms together with the outwardly facing evaporator surface 16 so to speak a guideway or channel for the particular partial water flow. How to proceed has already been explained, by this embodiment, the heat transfer surface of the Ice bank 30 and the evaporator approximately doubled. In favorable cases, the flow around Ice surface even more than doubles.
  • a second Frame profile 40b may be provided below and at least partially radially outside the ice bank 30 or the evaporator / Eisbank lake 16 is arranged.
  • This second Frame profile 40b can rest on the container bottom 22, and it can guide and Redirecting that partial water flow, the between the container wall 24 and the radially outwardly facing evaporator surface 16 flows.
  • the frame profile 40b can in substantially correspond to the frame profile 40a shown in Figures 5 and 6, so that The above with respect to these figures, the same applies analogously to the frame profile 40b.
  • This Transition must then be designed in a corresponding, suitable manner.
  • the first frame profile 40a must be spaced apart by suitable spacers Container bottom 22 and the second frame profile 40b are held.
  • the second frame profile 40b may be combined with the first frame profile 40a to form an overall structure be connected, as shown in the two representations of Figure 8.
  • the flow directing device 40 is a double-lead frame or baffle that functions as a unit can be used in the container 20 of the beverage cooling device.
  • the flow guide 40 from a wall be formed in the container 20 radially inside the evaporator surfaces 16 and under a distance, is arranged substantially parallel to these, wherein the wall in the substantially along the entire length of the evaporator surface 16 or much of it extends from it.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Devices That Are Associated With Refrigeration Equipment (AREA)
EP02732612A 2001-04-12 2002-04-12 Getränkekühlvorrichtung Expired - Lifetime EP1379822B1 (de)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DE10118622 2001-04-12
DE10118622A DE10118622C1 (de) 2001-04-12 2001-04-12 Getränkekühlvorrichtung
PCT/EP2002/004117 WO2002084188A1 (de) 2001-04-12 2002-04-12 Getränkekühlvorrichtung

Publications (2)

Publication Number Publication Date
EP1379822A1 EP1379822A1 (de) 2004-01-14
EP1379822B1 true EP1379822B1 (de) 2005-02-02

Family

ID=7681604

Family Applications (1)

Application Number Title Priority Date Filing Date
EP02732612A Expired - Lifetime EP1379822B1 (de) 2001-04-12 2002-04-12 Getränkekühlvorrichtung

Country Status (9)

Country Link
EP (1) EP1379822B1 (pt)
AT (1) ATE288574T1 (pt)
CZ (1) CZ296490B6 (pt)
DE (2) DE10118622C1 (pt)
ES (1) ES2237681T3 (pt)
HU (1) HUP0303982A3 (pt)
PT (1) PT1379822E (pt)
SK (1) SK286909B6 (pt)
WO (1) WO2002084188A1 (pt)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2419176B (en) * 2004-10-18 2009-04-08 Mf Refrigeration Ltd A Device for Cooling Liquids
GB2448621B (en) * 2006-07-08 2010-04-28 Imi Cornelius Beverage dispense
US20080202148A1 (en) * 2007-02-27 2008-08-28 Thomas Gagliano Beverage cooler
ITTO20130165A1 (it) * 2013-02-28 2014-08-29 Savese F Lli Ind S R L Vasca di raffreddamento per impianti di erogazione di bevande fredde
CN110075732A (zh) * 2019-04-04 2019-08-02 安徽猛牛彩印包装有限公司 一种印刷涂布液预热搅拌工艺装置

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2718236C2 (de) * 1977-04-23 1986-06-26 Hacheney, Wilfried, Dipl.-Ing., 4930 Detmold Verfahren zum Herstellen von hochkolloidalen Zement-Wasser-Gemischen
IE55764B1 (en) * 1983-11-16 1991-01-02 Coca Cola Co Post-mix beverage dispenser
GB8613958D0 (en) * 1986-06-09 1986-07-16 M K R Holdings Ltd Colling apparatus
US5368198A (en) * 1992-08-26 1994-11-29 Imi Cornelius Inc. Beverage dispenser
AUPN034694A0 (en) * 1994-12-30 1995-01-27 Comalco Aluminium Limited Improved draft tube agitator
IES70737B2 (en) * 1996-09-20 1996-12-11 Daniel Joseph Ryan An ice bank cooler system
GB2343243B (en) * 1998-10-28 2003-01-15 Imi Cornelius Beverage cooling
GB9912261D0 (en) * 1999-05-27 1999-07-28 Totton Manufacturing Limited Ice bank chillers

Also Published As

Publication number Publication date
DE50202171D1 (de) 2005-03-10
ES2237681T3 (es) 2005-08-01
EP1379822A1 (de) 2004-01-14
SK286909B6 (sk) 2009-07-06
DE10118622C1 (de) 2002-11-07
HUP0303982A2 (hu) 2004-03-29
WO2002084188A1 (de) 2002-10-24
CZ20032998A3 (cs) 2004-02-18
ATE288574T1 (de) 2005-02-15
CZ296490B6 (cs) 2006-03-15
HUP0303982A3 (en) 2008-05-28
SK13872003A3 (sk) 2004-02-03
PT1379822E (pt) 2005-06-30

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