EP1776178A1 - Procede et dispositif de carbonisation d'un liquide, de preference d'eau du robinet - Google Patents

Procede et dispositif de carbonisation d'un liquide, de preference d'eau du robinet

Info

Publication number
EP1776178A1
EP1776178A1 EP05774384A EP05774384A EP1776178A1 EP 1776178 A1 EP1776178 A1 EP 1776178A1 EP 05774384 A EP05774384 A EP 05774384A EP 05774384 A EP05774384 A EP 05774384A EP 1776178 A1 EP1776178 A1 EP 1776178A1
Authority
EP
European Patent Office
Prior art keywords
pump
arrangement
pressure
liquid
main
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
EP05774384A
Other languages
German (de)
English (en)
Other versions
EP1776178B1 (fr
Inventor
Margret Spiegel
Pasquale Spiegel
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
Priority to SI200531485T priority Critical patent/SI1776178T1/sl
Priority to PL05774384T priority patent/PL1776178T3/pl
Publication of EP1776178A1 publication Critical patent/EP1776178A1/fr
Application granted granted Critical
Publication of EP1776178B1 publication Critical patent/EP1776178B1/fr
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/60—Pump mixers, i.e. mixing within a pump
    • 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
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/236—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids specially adapted for aerating or carbonating beverages
    • B01F23/2363—Mixing systems, i.e. flow charts or diagrams; Arrangements, e.g. comprising controlling means
    • 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
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/237—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media
    • B01F23/2376—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media characterised by the gas being introduced
    • B01F23/23762—Carbon dioxide
    • B01F23/237621—Carbon dioxide in beverages
    • 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
    • B67D1/0042—Details of specific parts of the dispensers
    • B67D1/0057—Carbonators
    • B67D1/0058—In-line carbonators
    • 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
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/236—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids specially adapted for aerating or carbonating beverages
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S261/00—Gas and liquid contact apparatus
    • Y10S261/07—Carbonators

Definitions

  • the invention describes that carbonizing within one or more pump housing, preferably Co 2 with water.
  • the tap water pressure is increased by at least one fluid pressure increase pump and is forced under high pressure into a so-called carbonator kettle or pot.
  • Addition of Co 2 can carbonize. However, this always takes place by increasing the pressure within the Karbonatorkessels. So, you have to increase the fluid pressure.
  • Such a type of carbonization is mainly used in the dispensing industry for water dispensers and post-mix systems.
  • the so-called circulatory carbonators are also available to allow at least one, in technical terms, python to be used.
  • the so-called Pyton is nothing else, for example: syrup lines and gas line and still water line and also carbonation line, bundled and isolated from the carbonator to connect to the tap.
  • a carbonator kettle, tap water and Co 2 are carbonated via a booster pump within the boiler and this carbonated water is circulated.
  • the inventive solution is that one within a pump housing or more pump housing during operation of the pump, preferably carbonized
  • a positive displacement pump in use such as: the pump from the company Maprotec, which consists of a brass housing or VA steel housing.
  • These types of pumps are mainly used as a booster pump to, for example: fill a carbonator with water in the entrance area, for water.
  • the boiler is usually attached to one of these, which creates a backwater to the pump.
  • This back pressure causes the pump to do so because it can not displace the amount of water offered, but to maintain it by increasing the pressure inside the pump casing because the water can not be compressed, the space between the static component and the mechanical parts of the pumps inside a pressure increase, so that the pump can displace the offered amount of water for example to fill one or more Karbonatortöpfe.
  • the thus injected water with additions of preferably Co 2 in feeding the water is also added at the same time and with this carbonated liquid is then served at least one dispensing nozzle to remove carbonated liquid or at least produce a post-mix beverage.
  • the carbonated liquid which is in the Karbonatorkessel is used, for example, to supply a so-called Python with carbonated liquid. This usage is mostly applied to operation for post-mix. These are taps that have at least one inlet for carbonated liquid and at least one entrance for beverage syrups. These two liquids are mixed in the tapping process and so creates a preferred carbonated soft drink.
  • the invention now utilizes that by at least one pump, a carbonization is performed within the pump by giving on the input side of the pump for liquids, preferably Co 2 and tap water. This is usually absorbed even by the pump itself.
  • liquids preferably Co 2 and tap water.
  • Co 2 is with water within the pump housing to use the pump to provide the required pressure to be carbonized for this type of delivery
  • at least one line cross-sectional constriction is applied at the liquid and liquid conduit exit point Pump.
  • This liquid mixed with the applied principle with preferably Co 2 now carbonized with a high pressure from the pump exits. Because the high pressure within the pump housing arises when the cross-section reduction was completed before the pump outlet, inevitably because the pump has to displace the offered liquid offset with preferably Co 2 .
  • the carbonization within at least one pump housing has the advantage of carbonizing in the flow process, such as: an in-line carbonator.
  • the advantage of the invention is that when using the invention, the above-mentioned Karbonatorsysteme saves completely because in pumps Karbonatorsysteme the pump needed so that it also carbonates at the same time and not only circulating fluids and is needed to increase the pressure.
  • the invention has seen an even greater benefit on the material savings and energy consumption because Kreislaufkarbonatoren usually need at least two pumps for circulation operation and this are usually a booster pump to fill the Karbonatorkessel and operate the carbonation and at least one circulation pump order Keep fluid in circulation.
  • the booster pump and the complete Karbonatorsystem omitted, so save.
  • the preferred cross-sectional constriction of the conduit in which the preferred carbonated fluid is circulated is preferably applied prior to entry of liquids and gases to the pump since after cross-sectional constriction only the pressure provided by the water supply to the pump is present.
  • the cross-sectional constriction can also be introduced directly on the pump housing.
  • the pump (1) preferably VA steel pump housing, should preferably be operated via at least one electric motor.
  • At least one main liquid supply for the pump (1) is to be attached to the pump connection (3) (not shown) and at least one oasis supply preferably main supply.
  • tap water and gases, preferably Co 2 enter the liquid via the connection (3), the liquid and the gas can pass inside the pump housing (8).
  • the movable part of the pump (J) within the pump housing (8) displaces the liquid, preferably conveying Co 2 under pressure increase via the pump outlet (4) into the line (5).
  • the necessary increase in pressure is achieved, for example, by the cross-sectional constriction (6) in order to initiate the carbonation required by increasing the pressure within the pump housing (8) in order to remove carbonated liquid at least via a tapping point.
  • the carbonated water is up to the dispensing operation in the line (5) or is held during operation of the pump (1) in circulation and only in the dispensing new preferably tap water and preferably co 2 flow over the connection (3) of the pump ( 1) and can be carbonized in the pump housing (8).
  • FIG. 2 shows a schematically represented housing (1) made of preferably VA steel with at least one inlet possibility (4) for allowing tap water and Co 2 to flow into the housing (8) or into the housing by the suction force of the pump (1) Pull housing (8).
  • the component (16), the line (5) or the T-piece (5) is attached.
  • a cross-sectional constriction (6) is attached, which makes it possible with cycle carbonators (SO) to ensure that the dispensing process via preferably post-mix Hahne, (34) not too much carbonated liquid through the Kreislau ⁇ umpe ( 1) is pushed past the taps (34) during the tapping operation in order to guarantee the greatest possible volume flow, the taps (34).
  • SO cycle carbonators
  • the connection possibility (11) serves to connect the component (5) and inline carbonator (12) or the device (12) which preferably maintains tap water with Co 2 before entering the pump (1)
  • the component (13) ensures that preferably tap water and Co 2 via the possibility (14) (15) in the direction of inline carbonator (12) or mixer (12) preferably, filled with bulk material can flow and through the device (11) and the conduit (5) and the counselsm ⁇ ginate (4) in the pump housing (8) passes to the preferred to carbonize tap water and Co 2 by the pump inevitably builds up a high pressure on the cross-sectional constriction (6) on the outlet side for preferred carbonated liquids and then used to, for example: make soft drinks and via the lines (7) (5X1O) to the post-mix taps (34) to flow.
  • the outlet (3) for carbonated liquids can also be used for feeding, in this case, the entry possibility (4) is used to exit possibility for carbonated liquid.
  • the component (2) (not pictorially shown) can be used as overflow or relieving spill valve to an additional adjustment of the Baipasses or preferably used for pressure adjustment of the pump (1).
  • FIG. 17 shows: a schematic diaphragm electric pump (17) which can also be driven by gases.
  • the pump (17) has at least one liquid and gas inlet and outlet (21) and at least one liquid and gas outlet and inlet (18) and at least one chamber (20) which is used for carbonization and a pressure or Baipass setting (19) for preferred: tap water and Co 2 .
  • FIG. 1 shows: a schematic sketch of a pump (17) with theintuitsmögUchkeit about at least one inline premixer (12) dosed the inlet possibility (21) towards the pump inner housing (20) with preferably tap water and CcP to ensure it in that thereafter a continuous carbonization takes place within the pump housing (20)
  • the line (15) and the line (14) are suitable to supply the component (13) with preferably tap water and Co 2 , thus the liquid and the gas can get into the inline premixer (12) and via the device (11) and (30) through the opening (21) in the pump interior (19) pressure increased by the cross-sectional constriction (6) which causes the pump (1) (17) to increase the pressure for a good carbonization is required to force, because the pump, (1) (17) the liquid and the gas, through the cross-sectional constriction (6), presses.
  • an increase in pressure is made possible and the thus carbonated water can pass through the opening (18) on the pump (1) (17) in the line (5), through the interior of the line (10).
  • FIG. 1 shows a schematic sketch of a pump housing (I) 7 that an additional feed possibility (24) to gases or liquids or both together in addition to the entry possibilities (4) (3) for gases and liquids at or within the pump (1) in the direction Pump interior (8) with the Baipass option (2).
  • FIG. 1 shows: a schematic sketch of a pump housing (1) that has already been made at the factory with a bottleneck, preferably cross-sectional constriction (3) intended to ensure on the outlet possibility (3) the required high pressure in the pump (8) , This is ensured inside the pump housing (8) by previously known techniques such as: displacement mechanisms (not pictured)
  • FIG. 6 shows an additional Ba ⁇ teil (31) with a bore (25) which serves for cross-sectional constriction, which can be subsequently used in any conventional, preferably positive displacement pump (1) and roasted with the component (31), serving for Druckerh ⁇ hung.
  • FIG. 1 shows a schematic sketch of a Pumpengehauses (1) that at least one inline pre-mixer (12) inserted into the entry possibilities (3) (4) of the pump housing (1) in the direction of the pump chamber (8).
  • This in-line premixer (12) or in-line carbontor (12) is equipped with at least one device (32) which has the possibility of passing gases via the opening (28) and the opening (53) in the direction of inline (12) to ensure.
  • This method and structurally arranged can serve to use the pump (1) as a shock-carbonator pump (1), but also as a carbonator pump (1), inside the pump housing (8) with the components required for this, ( Figuratively not shown) carbonated and used at the same time as a circulation pump (1) if not tapped, because then no new pre-impregnated liquid can get into the pump interior. (Not pictured)
  • Co 2 in the direction of the inline premixer (12) is released via the opening (28), and tap water of the line (27) is preferably released via the opening (26) in the direction of the inline premixer (12).
  • carbonated liquid can be used for tapping and there is no gap of carbonated liquid in the lines (49X40) (6) (5) and preferably pumps - inner housings (8) and (20) and, as a result, there may also be no lack of liquid of carbonated liquid, such as: at the post-mix taps (34). (Not pictured)
  • the preferred bulk material (12) is preferably introduced into one or more hollow bodies (53) and is secured as a holder and securing of preferred sieve material (33).
  • the hollow body (53) has at least 2 openings (33) on the inflow and outflow, ensures fjk uncarbonated liquid or carbonated liquid.
  • FIG. 1 shows a schematic sketch of a top-counter post-mix dispensing system (38) with interesting carbonator system (12) (1) (17) and continuous cooling principle with still water precooling (42) which are also used as aftercooling (42) for still water may preferentially use the in-line pre-mixer (12) with preferentially cooled tap water for pre-carbonation and with at least one after-cooling line (40) for carbonated liquids, preferably tap water which may also be filtered (not shown pictorially) via line (44) in the preferential automatic pressure regulator (45), the doses over the existing fluid pressure, preferably the Co 2 pressure depending on the existing fluid pressure, dosed to the or inline pre-carbonator (12) to get into the pump (1X17) or may flow in conjunction with preferably tap water flowing from the mains through the automatic pressure regulator (45) Zapf process, and the existing flow pressure via a piston control (pictorially not shown) within the automatic pressure regulator with a differential pressure adjusted to the flow pressure of the liquid is used so that no Co 2 excess or too high
  • FIG. 1 shows: a schematic sketch of a circulatory carbonator principle, for preferential post-mix tap supply (34) with carbonated liquid via at least one tap water pressure regulator (44) may preferentially city water in the automatic pressure regulator for liquids and gases to flow, at the same time can preferably 2 Co which is stored in a Vorratsbehalter is (not shown pictorially) in the automatic pressure regulator (45) and flow out. Both media flow simultaneously via the lines (47) and (41) into the feed component (13) for the inline Vo ⁇ nischer (12).
  • the premixed media are sucked by the pump (8) with the aid of the pump (8) and the admission pressure of the two media, and are raised very high in the pump housing (8) and can be pumped via the outlet (3) of the pump (1)
  • the circulation circuit flow in and replace the previously removed amount of liquid, so that no Zapf interruption can take place.
  • the pump (1) serves to circulate the carbonated liquid in the circuit (49) and always cool through the refrigeration circuit (40) of which supply lines (48) go off to supply the valves (34) with carbonated liquid.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Devices For Dispensing Beverages (AREA)
  • Water Treatment By Sorption (AREA)
  • Non-Alcoholic Beverages (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)
  • Carbon And Carbon Compounds (AREA)

Abstract

Dans un boîtier de pompe (8), de l'eau provenant de préférence du robinet est carbonisée au moyen de CO2.
EP05774384A 2004-08-05 2005-07-29 Procede et dispositif de carbonisation d'un liquide, de preference d'eau du robinet Not-in-force EP1776178B1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
SI200531485T SI1776178T1 (sl) 2004-08-05 2005-07-29 Postopek in naprava za karbonizacijo tekočine, predvsem vodovodne vode
PL05774384T PL1776178T3 (pl) 2004-08-05 2005-07-29 Sposób i urządzenie do karbonizowania cieczy, zwłaszcza wody z wodociągu

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102004038563A DE102004038563A1 (de) 2004-08-05 2004-08-05 Verfahren und Anordnung zur Karbonisierung von Flüssigkeit mit CO2 innerhalb eines Pumpengehäuses
PCT/DE2005/001348 WO2006012874A1 (fr) 2004-08-05 2005-07-29 Procede et dispositif de carbonisation d'un liquide, de preference d'eau du robinet

Publications (2)

Publication Number Publication Date
EP1776178A1 true EP1776178A1 (fr) 2007-04-25
EP1776178B1 EP1776178B1 (fr) 2011-12-07

Family

ID=35159663

Family Applications (1)

Application Number Title Priority Date Filing Date
EP05774384A Not-in-force EP1776178B1 (fr) 2004-08-05 2005-07-29 Procede et dispositif de carbonisation d'un liquide, de preference d'eau du robinet

Country Status (11)

Country Link
US (4) US20070132114A1 (fr)
EP (1) EP1776178B1 (fr)
CN (1) CN101098748B (fr)
AT (1) ATE536217T1 (fr)
DE (1) DE102004038563A1 (fr)
DK (1) DK1776178T3 (fr)
ES (1) ES2381839T3 (fr)
PL (1) PL1776178T3 (fr)
PT (1) PT1776178E (fr)
SI (1) SI1776178T1 (fr)
WO (1) WO2006012874A1 (fr)

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GB2474741B (en) * 2009-08-21 2012-03-07 Schroeder Ind Inc Beverage dispensing apparatus
US8348243B2 (en) * 2010-03-14 2013-01-08 Sodastream Industries Ltd. Gas metering device for a home soda machine
US8567767B2 (en) 2010-05-03 2013-10-29 Apiqe Inc Apparatuses, systems and methods for efficient solubilization of carbon dioxide in water using high energy impact
US9309103B2 (en) 2010-05-03 2016-04-12 Cgp Water Systems, Llc Water dispenser system
EP2723481B1 (fr) 2011-06-23 2019-05-01 Apiqe Inc. Compensateur de flux
WO2012178179A2 (fr) 2011-06-23 2012-12-27 Apiqe Inc. Cartouche filtrante jetable destinée à un distributeur d'eau
US9033315B2 (en) 2011-10-11 2015-05-19 Flow Control Llc. Adjustable in-line on demand carbonation chamber for beverage applications
WO2016064794A1 (fr) * 2014-10-20 2016-04-28 Keurig Green Mountain, Inc. Circuit d'écoulement pour machine à boissons gazeuses
IL248295B (en) 2016-10-10 2018-02-28 Strauss Water Ltd Carbonation unit, system and method
EP3582662A4 (fr) 2017-02-15 2020-01-15 2266170 Ontario, Inc. Système de préparation et de percolation de boisson
US11554946B1 (en) 2022-03-21 2023-01-17 C18 Llc Supercharger and carbonated water mixing device
WO2023182974A1 (fr) * 2022-03-21 2023-09-28 C18 Llc Compresseur de suralimentation et dispositif de mélange d'eau gazeuse

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Also Published As

Publication number Publication date
DE102004038563A1 (de) 2006-03-16
US20090238938A1 (en) 2009-09-24
US20080142999A1 (en) 2008-06-19
SI1776178T1 (sl) 2012-06-29
PL1776178T3 (pl) 2012-07-31
PT1776178E (pt) 2012-03-22
ES2381839T3 (es) 2012-06-01
US20110081468A1 (en) 2011-04-07
CN101098748A (zh) 2008-01-02
EP1776178B1 (fr) 2011-12-07
CN101098748B (zh) 2012-07-18
DK1776178T3 (da) 2012-04-02
WO2006012874A1 (fr) 2006-02-09
ATE536217T1 (de) 2011-12-15
US8191867B2 (en) 2012-06-05
US20070132114A1 (en) 2007-06-14

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