EP2184257A1 - Installation de remplissage à chaud dotée d'une récupération de chaleur - Google Patents

Installation de remplissage à chaud dotée d'une récupération de chaleur Download PDF

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Publication number
EP2184257A1
EP2184257A1 EP09174042A EP09174042A EP2184257A1 EP 2184257 A1 EP2184257 A1 EP 2184257A1 EP 09174042 A EP09174042 A EP 09174042A EP 09174042 A EP09174042 A EP 09174042A EP 2184257 A1 EP2184257 A1 EP 2184257A1
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EP
European Patent Office
Prior art keywords
liquid
heat
heat exchanger
bottles
distributor
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
EP09174042A
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German (de)
English (en)
Other versions
EP2184257B1 (fr
Inventor
Danilo Schulz
Torsten Runge
Volker Richter
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.)
Krones AG
Original Assignee
Krones AG
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Publication date
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Application filed by Krones AG filed Critical Krones AG
Priority to PL09174042T priority Critical patent/PL2184257T3/pl
Publication of EP2184257A1 publication Critical patent/EP2184257A1/fr
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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67C—CLEANING, FILLING WITH LIQUIDS OR SEMILIQUIDS, OR EMPTYING, OF BOTTLES, JARS, CANS, CASKS, BARRELS, OR SIMILAR CONTAINERS, NOT OTHERWISE PROVIDED FOR; FUNNELS
    • B67C3/00—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus; Filling casks or barrels with liquids or semiliquids
    • B67C3/02—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus
    • B67C3/04—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus without applying pressure
    • B67C3/045—Apparatus specially adapted for filling bottles with hot liquids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B67—OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67C—CLEANING, FILLING WITH LIQUIDS OR SEMILIQUIDS, OR EMPTYING, OF BOTTLES, JARS, CANS, CASKS, BARRELS, OR SIMILAR CONTAINERS, NOT OTHERWISE PROVIDED FOR; FUNNELS
    • B67C3/00—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus; Filling casks or barrels with liquids or semiliquids
    • B67C3/02—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus
    • B67C3/06—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus using counterpressure, i.e. filling while the container is under pressure
    • B67C3/14—Bottling liquids or semiliquids; Filling jars or cans with liquids or semiliquids using bottling or like apparatus using counterpressure, i.e. filling while the container is under pressure specially adapted for filling with hot liquids

Definitions

  • the invention relates to a hot filling plant for a liquid, in particular a beverage, with heat recovery, with a heat exchanger for preheating the liquid to a first temperature; a heater downstream of the heat exchanger for heating the liquid to a second temperature higher than the first temperature; with a first distributor connected downstream of the heater for dividing the liquid into, for example, a portion to be filled into bottles, jars, bags or the like and a portion attributable to the inlet of the heat exchanger; with a bottle filler connected downstream of the first distributor for filling the liquid in bottles; and with a first distributor downstream of the recooler for cooling the portion to be recycled.
  • the hot filling after pasteurization, z. B. in a short-term heater, is a proven method to fill drinks durable in bottles or bags.
  • the untreated drink is usually preheated, degassed and then pasteurized.
  • z. B. After bottling, z. B. at 85 ° C, the filled bottles in a bottle cooling by means of a coolant flow, z. B. by sprinkling, suitable for further processing temperature of z. B. 30 ° C cooled.
  • piggable Pasteurstrom with continuous vacuum degassing, liquid fruit, 8/2002, 508-510 is known to cool down in the hot filling of beverages, especially at a standstill of the bottle filler, already pasteurized liquid in a recooler and a buffer of untreated Re-mix liquid.
  • the withdrawn the filled bottles or bags heat is z. B. passed into a heat exchanger for preheating the liquid to be treated.
  • the heat removed during the re-cooling of the unfilled liquid is disposed of in known hot filling plants in a cooling tower and is an energy loss to book. This is also to be considered in trouble-free normal operation when a certain proportion of the heated, not yet bottled liquid is recooled and the untreated liquid is mixed again to stabilize the operation of the system.
  • the invention has the object of the reason to reduce the energy loss during hot filling in comparison to the known systems.
  • the liquid can be preheated with heat obtained during the re-cooling and the energy losses can be reduced.
  • the first distributor directs the liquid at a standstill of the bottle filler substantially completely through the recooler. This maximizes the amount of energy available for recovery.
  • the hot filling plant comprises a second distributor which adjusts the portion of the heat transport medium to be fed from the recooler into the heat exchanger.
  • the heat output to be transmitted can be metered in a targeted manner.
  • the first distributor divides the liquid during operation of the bottle filler so that the proportion attributable to 10 - 15% of the portion to be filled. This ensures a stable control of the system.
  • the hot filling plant further comprises a bottle cooler for cooling the filled bottles, the return of which is connected to the flow of the heat exchanger, to heat energy from the bottle cooler to the heat exchanger transfer.
  • a bottle cooler for cooling the filled bottles, the return of which is connected to the flow of the heat exchanger, to heat energy from the bottle cooler to the heat exchanger transfer.
  • the H fostab garllstrom further comprises a third manifold, the heat transfer means from the return of the bottle cooler optionally passes into the heat exchanger or the flow of the bottle cooler.
  • the amount of heat recovered can be selectively controlled or the heat transport medium can be circulated as needed.
  • the third distributor directs the heat transfer agent from the return of the bottle cooler in the flow of the bottle cooler when no bottles are cooled in the bottle cooler. This delays unwanted cooling of the bottle cooler.
  • the flow temperature of the heat exchanger 50 - 80 ° C. This allows a particularly effective heat recovery.
  • the underlying object is further achieved by a method for hot filling of liquids according to claim 9.
  • the liquid is preheated with heat energy recovered by re-cooling the portion to be recycled.
  • the portion to be returned is set to be 10 to 15% of the portion to be filled during bottling. This ensures a stable control of the system.
  • the liquid is completely returned at an interruption of the bottling. This maximizes the amount of energy available for recovery.
  • the method further comprises the steps of: cooling the filled bottles; and preheating the liquid with heat energy recovered as the bottles cool.
  • the released during cooling heat energy can be recovered and used again to heat the liquid.
  • the liquid is preheated with thermal energy obtained as the bottles cool and with thermal energy recovered upon cooling.
  • thermal energy obtained as the bottles cool and with thermal energy recovered upon cooling.
  • the thermal energy obtained during cooling of the bottles is only used for preheating the liquid as long as bottles are cooled. This avoids that a device used for bottle cooling cools down quickly.
  • FIG. 1 schematically shows a hot filling plant 1 for a liquid 2, in particular for a drink.
  • the dashed arrows indicate the flow direction of the liquid 2 again
  • the solid arrows indicate the flow direction of a heat transfer medium 3, such. B. water.
  • the hot filling plant 1 accordingly comprises a collecting container 4 for temporarily storing the liquid 2 to be treated and to be filled, which in turn comprises a heat exchanger 6, a preheater 8, a heater 10 and a first adjustable three-way distributor 12 having an inlet 12a and two exits 12b and 12c are connected downstream.
  • the heat exchanger 6 comprises an inlet 6a and an outlet 6b for the liquid 2 and a flow 6b and a return 6c for the heat transport medium 3 and preheats the liquid 2 to a preheating temperature T V , the z. B. is required for a conventional degassing of the liquid in a (not shown) degassing.
  • the preheater 8 the liquid 2 additionally pre-heated, for. B. inadequate heat output of the heat exchanger 6 or during startup of the system. 1
  • the liquid 2 is heated to a treatment temperature T B which is higher than the preheating temperature T V.
  • the first distributor 12 divides the liquid 2 flowing out of the heater 10 into a portion F A to be filled and a portion F R attributable to the product circuit or collecting container 4.
  • the output 12b of the first distributor 12 is followed by a bottle filler 14, which fills the liquid component F A into bottles 16.
  • the output 12c is followed by a recooler 18 having an inlet 18a and an outlet 18b for the liquid 2, as well as a feed 18c and a return 18d for the heat transporting means 3.
  • the outlet 18b of the recooler 18 leads back to the collecting container 4.
  • the recooler 18 forms with a second adjustable three-way manifold 20, the heat exchanger 6 and a first cooling tower 22, a first heat transfer medium circuit 24.
  • the input 20a of the second manifold 20 is fed from the return 18 d of the recooler 18 and divides the flow of the heat transfer medium 3 in a share W E for external heat disposal in the first cooling tower 22 and a share W R for heat recovery in the heat exchanger 6. Accordingly, an output 20b of the second distributor 20 is connected to the flow of the first cooling tower 22, the other output 12c to the flow 6c of the heat exchanger 6.
  • the hot filling plant 1 further comprises a bottle cooler 28 for cooling the filled bottles 16.
  • This comprises a supply line 28c and a return line 28d for the heat transporting means 3 and forms with a third adjustable three-way distributor 30, the heat exchanger 6 and a second cooling tower 32, a second heat transfer medium circuit 34.
  • the input 30a of the third distributor 30 is fed from the return line 28d of the bottle cooler 28 and passes the heated in the bottle cooler 28 heat transport means 3 in a first position via the output 30b to the flow 6c of the heat exchanger 6 to heat energy from the bottle cooler 28 for Heat exchanger 6 to transfer.
  • the third distributor 30 short-circuits the flow 28c and the return 28d of the bottle cooler 28 via the outlet 30c.
  • the liquid 2 is z.
  • a drink e.g. Water, milk, juice, beer, lemonade or any other liquid that is treated by heat and filled in the heated state.
  • the liquid may include an emulsion, suspension and / or a foam.
  • the heat exchanger 6 may, for. Example, be a conventional plate or tubular heat exchanger and is preferably operated at a flow temperature of 50 to 80 ° C.
  • both heat transport medium circuits 24 and 34 are in each case connected in parallel to the supply line 6c and the return line 6d.
  • the circuits could also be separated from each other, z. B. by check valves, by a separate flow and return 6c, 6d for each circuit or by a two-stage design of the heat exchanger 6. It is crucial that both circuits 24, 34 used for preheating the liquid 2 and can be combined and optimized if necessary , Likewise, the cooling towers 22 and 32 or their cooling capacity and the respective volume flows could deviate from FIG. 1 be interconnected or regulated, as long as they fulfill the function described.
  • the preheater 8 may, for. B. be heated with steam.
  • the heater 10 is, for example, a conventional, steam-operated, short-lived, heat-retaining heater in which the liquid 2 to be treated is kept at the treatment temperature T B for a certain duration, e.g. B. for pasteurization.
  • the heater 10 may include a correction cooler (not shown) to adjust the treated liquid 2 to a suitable temperature for bottling, such as a bottle. B. 85 ° C, adjust.
  • the amount of heat withdrawn from the liquid 2 is returned as far as possible to the inlet of the heater 10 in order to heat the inflowing liquid 2.
  • the distributor 12 is z. B. an electrically controlled mixing valve, with which the liquid fractions F R and F A can be graded as finely as possible in relation to each other or continuously changed as can also be adjusted so the liquid 2 is conducted exclusively to the bottle filler 14 or to the recooler 18.
  • the bottle filler 14 fills the heated liquid 2 supplied to it continuously in bottles 16 in a conventional manner.
  • the bottles 16 may, for. B. made of glass or plastic.
  • other containers such. B. bag, to be filled.
  • the filled bottles 16 are in the bottle cooler 28 z. B. by sprinkling with water to a temperature suitable for further processing, such. B. 30 ° C, cooled.
  • the bottle cooler 28 may, for. B. be designed as a multi-stage cooling tunnel.
  • the bottle cooler 28 is designed so that the highest possible return temperature is achieved, for. B. in the range of 50 to 80 ° C to optimize the efficiency of heat recovery at the heat exchanger 6. This can be z. B. by a suitable design of individual cooling stages of the cooling tunnel and / or by increasing the residence time of the bottles 16 in the bottle cooler 28 or by reducing the volume flow of the heat transfer medium 3 through the bottle cooler 28th
  • the third distributor 30 is preferably an electrically controlled switching valve that either passes the heated heat transfer medium 3 flowing out of the return 28d of the bottle cooler 28 completely to the inlet 6c of the heat exchanger 6 or, in short-circuit operation, returns it to the inlet 28c of the bottle cooler 28.
  • the short-circuit operation prevents or delays the cooling of the bottle cooler 28 if temporarily no filled bottles 16 arrive at the bottle cooler 28.
  • the third distributor 30 could also be designed as a mixing valve.
  • the recooler 18 is preferably designed so that the highest possible return temperature is achieved, for. B. 50 - 80 ° C in order to achieve the highest possible efficiency of heat recovery at the heat exchanger 6.
  • the liquid 2 is intended to be cooled approximately to the temperature of the untreated liquid 2, for example to a temperature of about 20-40 ° C, before it mixes in the collecting container 4 with untreated liquid 2.
  • liquid 2 is continuously passed through the heat exchanger 6 and thereby heated to a preheating temperature T V. If the heat output of the heat exchanger 6 is insufficient, the liquid 2 in the preheater 8 is additionally heated up to the temperature T V.
  • the liquid 2 is then z. B. by a (not shown) vacuum degassing and / or other processes and passed to the heater 10. In this, the liquid 2 z. B. for pasteurization for a certain period of time to a treatment temperature T B , where: T B > T V.
  • a portion F A of the treated liquid 2 is passed into the bottle filler 14 and bottled in this at a temperature of preferably 80-90 ° C in bottles 16.
  • the remaining portion F R of the treated liquid 2 is passed into the recooler 18, cooled in this to 20 - 40 ° C and returned to the sump 4.
  • the proportionate return of the liquid 2 in normal operation ensures stable operation of the filling plant. In this way, z. Example, be avoided that liquid 2 due to lack of sterility in a delayed filling must be discarded.
  • the ratio F R / F A is 0.05 - 0.2 in normal operation.
  • a ratio F R / F A of 0.1-0.15 is preferred.
  • the ratio of the heat transfer medium circuits 24 and 34 respectively at the returns 18d and 28d available heat outputs in normal operation corresponds approximately to the ratio F R / F A.
  • the heat recovery in the bottle cooler 28 and in the recooler 18, or in the heat medium circuits 34 and 24, can be combined to minimize the energy losses of the filling system 1 in normal operation and / or to optimize their control.
  • the entire heated liquid 2 is possible under the conditions of normal operation to cycle in order to continue the filling process quickly.
  • FIG. 2 shows the potential for energy recovery in the circuits 24 and 34 available heat output during operation B and during a temporary stoppage S of the bottle filler 14. In normal operation are each substantially constant in time amounts of heat from the circuits 24 and 34 are available.
  • the entire liquid 2 is passed from the first manifold 12 in the recooler 18 and cooled in this approximately to the starting temperature of the untreated liquid 2.
  • the heat output available at the return 18d of the recooler 18 increases until it corresponds to the output of the bottle cooler 14 during normal operation.
  • the third distributor 30 closes the supply line 28 c and the return line 28 d of the bottle cooler 28 at the instant S 'and at the same time prevents the supply 28 c from the second cooling tower 32 from being fed.
  • the heat output available overall on the heat exchanger 6 may temporarily fall below a minimum value necessary for preheating the liquid 2, so that additional heat output must be applied by the preheater 8 for this purpose.
  • the liquid 2 can be preheated mainly by recovered energy and additional, external energy input compared to conventional systems can be significantly reduced.

Landscapes

  • Filling Of Jars Or Cans And Processes For Cleaning And Sealing Jars (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
  • Heat-Pump Type And Storage Water Heaters (AREA)
  • Coating With Molten Metal (AREA)
  • Steam Or Hot-Water Central Heating Systems (AREA)
EP09174042A 2008-11-10 2009-10-26 Installation de remplissage à chaud dotée d'une récupération de chaleur Active EP2184257B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL09174042T PL2184257T3 (pl) 2008-11-10 2009-10-26 Instalacja do rozlewu na gorąco z odzyskiwaniem ciepła

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE102008056597A DE102008056597A1 (de) 2008-11-10 2008-11-10 Heißabfüllanlage mit Wärmerückgewinnung

Publications (2)

Publication Number Publication Date
EP2184257A1 true EP2184257A1 (fr) 2010-05-12
EP2184257B1 EP2184257B1 (fr) 2011-09-07

Family

ID=41698368

Family Applications (1)

Application Number Title Priority Date Filing Date
EP09174042A Active EP2184257B1 (fr) 2008-11-10 2009-10-26 Installation de remplissage à chaud dotée d'une récupération de chaleur

Country Status (8)

Country Link
US (1) US8356643B2 (fr)
EP (1) EP2184257B1 (fr)
CN (1) CN101734591B (fr)
AT (1) ATE523465T1 (fr)
DE (1) DE102008056597A1 (fr)
DK (1) DK2184257T3 (fr)
ES (1) ES2369054T3 (fr)
PL (1) PL2184257T3 (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2567935A1 (fr) * 2011-09-07 2013-03-13 Krones AG Procédé et dispositif de chauffage dýun produit sýécoulant
EP3114204B1 (fr) 2014-03-04 2018-08-08 ZIEMANN HOLVRIEKA GmbH Procédé et dispositif de préparation d'un aliment liquide
CN109843782A (zh) * 2016-09-12 2019-06-04 克朗斯股份公司 用于对液体进行热处理和灌装的灌装线
DE102020127542A1 (de) 2020-10-20 2022-04-21 Krones Aktiengesellschaft Abfüllanlage und Verfahren zur Heißabfüllung eines flüssigen Produkts in Behälter

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102008048812A1 (de) * 2008-09-24 2010-04-01 Khs Ag Verfahren und Vorrichtung zur kombinierten Herstellung und Abfüllung von Behältern aus Kunststoff
DE102008056597A1 (de) 2008-11-10 2010-05-12 Krones Ag Heißabfüllanlage mit Wärmerückgewinnung
SE534448C2 (sv) * 2010-04-13 2011-08-23 Tetra Laval Holdings & Finance Metod och anordning för att återvinna energi vid varmfyllning av en flytande livsmedelsprodukt
DE102011007787A1 (de) * 2011-04-20 2014-01-16 Krones Aktiengesellschaft Vorrichtung und Verfahren zum Behandeln eines flüssigen Lebensmittelproduktes
DE102012219759A1 (de) * 2012-10-29 2014-04-30 Krones Ag Wärmerückgewinnung aus Tunnelrückkühlerprozess
DE102014100733A1 (de) * 2014-01-23 2015-07-23 Krones Ag Kühlsystem für Behälterbehandlungsanlagen
DE102019126946A1 (de) * 2019-10-08 2021-04-08 Krones Aktiengesellschaft Verfahren und Vorrichtung zur Heißabfüllung von flüssigem Produkt

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EP1598308A1 (fr) * 2002-12-12 2005-11-23 Suntory Limited Procede et dispositif de chargement de liquide
DE102005053005A1 (de) 2005-11-05 2007-05-10 Kelterei Walter Gmbh & Co. Kg Verfahren und Vorrichtung zum Abfüllen von Getränken

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DE102008056597A1 (de) 2008-11-10 2010-05-12 Krones Ag Heißabfüllanlage mit Wärmerückgewinnung

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Publication number Priority date Publication date Assignee Title
EP1598308A1 (fr) * 2002-12-12 2005-11-23 Suntory Limited Procede et dispositif de chargement de liquide
DE102005053005A1 (de) 2005-11-05 2007-05-10 Kelterei Walter Gmbh & Co. Kg Verfahren und Vorrichtung zum Abfüllen von Getränken

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2567935A1 (fr) * 2011-09-07 2013-03-13 Krones AG Procédé et dispositif de chauffage dýun produit sýécoulant
US10039295B2 (en) 2011-09-07 2018-08-07 Krones Ag Method and device for heating a liquid product
EP3114204B1 (fr) 2014-03-04 2018-08-08 ZIEMANN HOLVRIEKA GmbH Procédé et dispositif de préparation d'un aliment liquide
CN109843782A (zh) * 2016-09-12 2019-06-04 克朗斯股份公司 用于对液体进行热处理和灌装的灌装线
DE102020127542A1 (de) 2020-10-20 2022-04-21 Krones Aktiengesellschaft Abfüllanlage und Verfahren zur Heißabfüllung eines flüssigen Produkts in Behälter
EP3988498A1 (fr) * 2020-10-20 2022-04-27 Krones AG Usine de remplissage et procédé de remplissage à chaud d'un récipient d'un produit liquide

Also Published As

Publication number Publication date
ATE523465T1 (de) 2011-09-15
EP2184257B1 (fr) 2011-09-07
ES2369054T3 (es) 2011-11-24
DE102008056597A1 (de) 2010-05-12
US20100139214A1 (en) 2010-06-10
DK2184257T3 (da) 2011-12-12
US8356643B2 (en) 2013-01-22
CN101734591B (zh) 2012-09-05
PL2184257T3 (pl) 2012-02-29
CN101734591A (zh) 2010-06-16

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