EP1809577A1 - Procede et installation de carbonation d'un liquide - Google Patents

Procede et installation de carbonation d'un liquide

Info

Publication number
EP1809577A1
EP1809577A1 EP05769763A EP05769763A EP1809577A1 EP 1809577 A1 EP1809577 A1 EP 1809577A1 EP 05769763 A EP05769763 A EP 05769763A EP 05769763 A EP05769763 A EP 05769763A EP 1809577 A1 EP1809577 A1 EP 1809577A1
Authority
EP
European Patent Office
Prior art keywords
main
arrangement
liquid
liquids
pressure drop
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.)
Withdrawn
Application number
EP05769763A
Other languages
German (de)
English (en)
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
Publication of EP1809577A1 publication Critical patent/EP1809577A1/fr
Withdrawn legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
    • 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
    • B01F23/2362—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids specially adapted for aerating or carbonating beverages for aerating or carbonating within receptacles or tanks, e.g. distribution machines
    • 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
    • B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
    • B01F35/90—Heating or cooling systems
    • B01F35/92—Heating or cooling systems for heating the outside of the receptacle, e.g. heated jackets or burners
    • 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

Definitions

  • the invention shows a method by the DruckabfeU that arises in the Stillwasser- cycle when at least one tap is connected to the Stillwasser- cycle and is tapped from the supply of liquids of the Stillwasser- cycle.
  • the pressure drop in the mains network is used to supply at least one in-line carbonator with liquids to carbonize during the tapping process, preferably Co 2 with tap water.
  • the Leitiganguhr pressure is increased by at least one fluid pressure increase pump and is pressed at high pressure in a so-called Karbonatorkessel or pot. Addition of Co 2 can carbonize. However, this always takes place by increasing the pressure inside the carbonator shell. 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.
  • This carbonated water with the help of a circulation pump, always in the direction of the taps, in a circuit, kept in motion and runs over and over again a cooling for liquids to keep the carbonated water at an ideal tapping temperature to produce post-mix drinks .
  • two pumps are needed, a Druckh ⁇ hungspumpe to carbonize, and a circulation pump to keep carbonated water in circulation.
  • One of these pumps can also run the still water cycle to recycle non-enriched tap water around this still water circuit, which is also used primarily to cool syrup or used to mix carbonated water with still water. All the above mentioned pipes are bundled and insulated.
  • the invention saves at least one pump, in the aforementioned method or other methods and also the circulation lines for carbonated liquid, fall away. Because the invention uses the pressure drop to carbonize the tapping process, which inevitably occurs.
  • the are connected to one or more circulation pumps to the still water to be pumped in the circuit has at least one supply connection to one or more main supply for liquids, preferably tap or mineral water.
  • the pressure drop takes place in the circuit, at least one pump, fresh water can flow or sucked at least one pump and be prompted by the pressure increase of the pump in the flow line in the direction of tap or points to, for example: the stillwater circuit for the Use cooling of syrups and carbonation to ensure that the pressure drop within the circuit of the circulation lines, which is preferably introduced in a preferably, for example: Python, is kept constant in order to have a constant pressure drop controlled by the
  • the invention makes use of the following:
  • the fluid pressure in the circulation line is kept constant. This may, but is not strictly necessary, be set directly at the pump.
  • the pressure drop inevitably arises because water is an inertial mass and inevitably the lower Resistance follows, which is when tapping in the direction of tap or taps, is used so that the liquid in the direction of inline carbonator or in general in any device that can be 'used for carbonization''liquid is supplied.
  • This liquid is simultaneously mixed with gas, preferably Co 2 or enriched or mixed and can then simultaneously flow through the preferred in-line carbonator and get to the one or more taps to preferably produce and tap non-alcoholic soft drinks. This is commonly known as the post-mix method.
  • in-line Karbopnator in the flow process, because in the reverse bend, which is the flow line or lines connected to the Return line or lines, in turn, with the or the Kreislau ⁇ umpen preferred: positive displacement pump, is connected and provided with at least one additional outlet to preferably: inline carbonator or carbonators with liquids to supply.
  • the tapping process When the tapping process is finished, carbonation is no longer possible. Because up to the taps, a pressure equalization has taken place and now the liquid is circulated only in the still water cycle. Also, the new fluid supply then rests from the main water supply, towards the pump. At least one backflow preventer is inserted or interposed in the return line, in order to force downstream water from the main supply to flow in the direction of the pump, in order to guarantee the pump suction flow direction. Also, at least one pressure regulator should be provided between the main supply line for the liquid and the pump, which if possible also cleans the liquids before a filter system.
  • the aforesaid still water cycle can also be used, for example, to supply two or more preferred in-line carbonators with liquids to utilize the pressure drop within the lines to carbonize.
  • the liquid main supply (13) has at least one connection possibility for a pressure limiter (21) in the line (16), at least one - bunkmannbegrenzer (12) can be intregiert.
  • the line (16) is connected to the line (9), in which at least one backflow preventer (12) is mounted in the flow direction to open the pump (15).
  • the lines (9) (16) are at the connection possibility (14) of the pump (15) there to use ⁇ to the liquid supply to the pump (15) and the still water circuit (9) (10) consisting of the following components: Reverse bend (7) with at least one outlet (8) of the return line (9) with intreg convinced backflow preventer (12) with connection option (16) and the intreg striv backflow preventer (12) is intregiert on the supply line (16).
  • the pump connection (14) is connected to the line (16) and the return line (9),
  • the pump connection (17) which serves for the circuit (9) (10) and which also serves to fill the circuit cooling coil (23) for liquids in order to connect the connections (17) to the line (23), preferably screwed (not shown in the drawing).
  • the coolant line (23) is used for connection via the connection possibility (22) to the connection (10) via the connection possibilities (11), the still water circuit is produced which is guaranteed when the tap points (1) are not open.
  • the liquid supply via the port (6) of the Iriline carbonator (5) take place to pressure drop, which takes place when at least one tap (l) is opened.
  • the sluggish amount of liquid on the reverse bend (7) reach the outlet (8) via the connection possibility (6) in the carbonator (5).
  • preferably Co 2 gas can flow via the connection (20) into the inline carbonator (5) and leave the preferably inline carbonator via the outlet (4).
  • the liquid, preferably tap water offset with preferably Co 2 is in the flow through the carbonator (5) the fluids and Co 2 carbonized.
  • This carbonated liquid is then passed on via the outlet (4) preferably via at least one distributor (3) which takes over the distribution of carbonated liquids via at least one line (2) to at least one tap (1) which the removal of carbonated liquids makes possible.
  • the gas supply (20) is connected to at least one main gas supply. (Not pictured) To cool the liquids, state of the art is applied (not pictured)
  • the pump (15) is preferably a Trennschieber- positive displacement pump, the deri constructed fluid pressure via the outlet (17) further in the direction of cooling (23) continues to give and forwards in the direction preferably inline carbonator (5) and at least one tap (1) ,
  • tapping creates a pressure drop within the StiHwassernikonnees (9) (10) passing at this moment on the main liquid supply (13) via the pressure regulator (21) pass through the backflow preventer (12) pass through at least one filter system. (Not pictured) Then the liquid flows via the line (16) in the direction of the pump (15) via the connection (14) of the pump (15).
  • the still water circuit (9) (10) is always refilled with the amount of liquid that is removed during the tapping to the liquids, preferably tap water, cooled to at least one tapping point (1) to provide. Pumps the pump (15) in the direction of cooling (23) and builds up the pressure in the direction.
  • the invention uses the slide valve pumps (15) can be self-priming. This, in turn, guarantees that the still water circuit (9) (10) is filled because it is not always possible to find such a high fluid pressure on site as to guarantee the liquid main supply (13) with fluid of the circuit (9) (10) is because to fill the circuit (9) (10) again with liquids. It is advantageous to use a self-priming pump (15).
  • cooling (18) may also be stationed at a location other than the location of the carbonisation (5) or tap (l) or main connection (13) , (Not pictured)
  • the still water circuit (9) (10) can also be used for cooling beverage additives. (Not pictured)
  • the Stülwasserniklauftechnischen (9) (10) and reversal sheets (7) are bundled with beverage additive lines and isolated in at least one so-called Pyton introduced or similar methods apply. (Not shown) This would have the advantage that in a simple way also to cool the beverage supplements for post-mix drinks.
  • the beverage additives which can be transported independently in lines separately to at least one tapping point (1) and pre-cooled (not pictured)
  • FIG. 2 shows the same principle as FIG. 1, with the difference that two preferably in-line carbonators (5) are supplied by a still water circuit (9) (10) of cooled or uncooled liquid. Insulated into at least one bundle, more such as a stillwater circuit (9) (10) can be introduced around the stillwater circuits (9) (10) including the preferred in-line carbonator (5) or carbonators (5) with the components (3 ) Distributor (3) and the carbonated liquid outlet (4) and the lines (2) and the taps (2) or tapping point (1) preferably post-mix taps (1) to clean, there is one or more connections to separate the necessary For flushing with preferably tap water, the main supply (13) for liquids is used and withdrawn via the tapping point (1) or the taps (1) until the rinsing process has been carried out ) or pump (15), at least one additional still water circuit (9) (10) can be used for the purpose of accompanying refrigeration cycle. (BilcUich not shown)

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Devices For Dispensing Beverages (AREA)

Abstract

L'invention concerne un procédé qui utilise la chute de pression survenant dans le système de circulation d'une eau plate lorsqu'au moins une prise d'eau est reliée à ce système de circulation et retirée du réservoir de liquides dudit système de circulation. A ce moment, la chute de pression dans le système de conduites est utilisée pour alimenter en liquide au moins un appareil de carbonation en ligne, pour engendrer la carbonation, de préférence d'eau de robinet à l'aide de CO<SUB>2</SUB>, pendant le processus de retrait.
EP05769763A 2004-07-28 2005-07-22 Procede et installation de carbonation d'un liquide Withdrawn EP1809577A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102004036679A DE102004036679A1 (de) 2004-07-28 2004-07-28 Nach Verfahren und Anordnung dadurch gekennzeichnet: das durch Druckabfall in mindestens einer Flüssigkeitsleitung den entstehenden Druckabfall zu nutzen, um mindestens einen Karbonisierungsprozess mit der anfallenden Flüssigkeit in Verbindung mit bevorzugt Co2 anzuwenden
PCT/DE2005/001306 WO2006012850A1 (fr) 2004-07-28 2005-07-22 Procede et installation de carbonation d'un liquide

Publications (1)

Publication Number Publication Date
EP1809577A1 true EP1809577A1 (fr) 2007-07-25

Family

ID=34973258

Family Applications (1)

Application Number Title Priority Date Filing Date
EP05769763A Withdrawn EP1809577A1 (fr) 2004-07-28 2005-07-22 Procede et installation de carbonation d'un liquide

Country Status (3)

Country Link
EP (1) EP1809577A1 (fr)
DE (1) DE102004036679A1 (fr)
WO (1) WO2006012850A1 (fr)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE202007003204U1 (de) * 2007-03-05 2007-07-19 Ds Produkte Dieter Schwarz Gmbh Vorrichtung zum Begasen von Leitungswasser

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19614754C1 (de) * 1996-04-16 1997-06-05 Duesseldorf Stadtwerke Kühlen und CO¶2¶-Anreichern von Trinkwasser
GB9824110D0 (en) * 1998-11-04 1998-12-30 Imi Cornelius Uk Ltd Carbonation
DE19947822A1 (de) * 1999-10-05 2001-04-12 Linde Gas Ag Verfahren und Vorrichtung zur Abgabe von carbonisiertem Trinkwasser über einen Wasserhahn

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2006012850A1 *

Also Published As

Publication number Publication date
DE102004036679A1 (de) 2006-03-23
WO2006012850A1 (fr) 2006-02-09

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