EP2476492B1 - Installation de nettoyage de récipient - Google Patents

Installation de nettoyage de récipient Download PDF

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Publication number
EP2476492B1
EP2476492B1 EP11194229.8A EP11194229A EP2476492B1 EP 2476492 B1 EP2476492 B1 EP 2476492B1 EP 11194229 A EP11194229 A EP 11194229A EP 2476492 B1 EP2476492 B1 EP 2476492B1
Authority
EP
European Patent Office
Prior art keywords
stage
heat
heat exchanger
pretreatment
cleaning
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.)
Active
Application number
EP11194229.8A
Other languages
German (de)
English (en)
Other versions
EP2476492A1 (fr
Inventor
Karl-Heinz Messer
Holger Joost
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
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Krones AG
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Publication date
Application filed by Krones AG filed Critical Krones AG
Publication of EP2476492A1 publication Critical patent/EP2476492A1/fr
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Publication of EP2476492B1 publication Critical patent/EP2476492B1/fr
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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B08—CLEANING
    • B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B9/00—Cleaning hollow articles by methods or apparatus specially adapted thereto 
    • B08B9/08—Cleaning containers, e.g. tanks
    • B08B9/20—Cleaning containers, e.g. tanks by using apparatus into or on to which containers, e.g. bottles, jars, cans are brought
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B08—CLEANING
    • B08B—CLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B13/00—Accessories or details of general applicability for machines or apparatus for cleaning

Definitions

  • the invention relates to a container cleaning system explained in the preamble of claim 1 Art.
  • Container cleaning systems such as cleaning systems for reusable containers in the beverage industry, are relatively energy consuming in operation. These container cleaning systems usually contain a plurality of treatment stages, in which the containers are treated with cleaning agent or cleaning liquor, wherein in most treatment stages, the cleaning agent must have an elevated temperature. Since the detergent is subsequently discarded, that is supplied to the wastewater, efforts are already known, for example from the DE 32 05 956 to operate these container cleaning systems energy-saving, in particular heat energy-saving. However, the approach to an energy-saving design is in the known container cleaning systems in the recovery of waste heat. In contrast, the heating of the treatment liquids in a conventional manner, ie, for example, by a fuel-fired heater or the like.
  • a device for supplying energy to a brewery which comprises means for converting a biogas into thermal and electrical energy and means for providing a residual requirement of electrical and thermal energy from regenerative sources.
  • the invention has for its object to operate a container cleaning system energy-saving.
  • the present invention proposes a way to circumvent one of these limits.
  • Combined heat and power plants can generally handle no small temperature differences. They would therefore only of limited suitability for heat cycles for heating a main cleaning stage in a container cleaning plant, since after the heating of the treatment liquid in the main cleaning stage, the return is cooled to only about 83 ° C.
  • the combined heat and power plant can process this relatively low-cooled heat medium only poorly.
  • a pretreatment stage as reflux cooler to operate the return temperature can be lowered so far, preferably to about 70 ° C or less, that the cogeneration plant can better handle the return.
  • the supply of the main cleaning stage and / or the pretreatment stage via heat exchangers represents the simplest design possible.
  • the heat exchanger of the pretreatment stage is designed for a predetermined temperature reduction or to a predetermined starting temperature.
  • a bypass line of the heat exchanger of the pretreatment stage makes sense, should be required for the main cleaning stage, an amount of energy that is greater than the usual amount of energy, so that a return cooling is not required and / or not efficient.
  • the container cleaning installation 1 contains the customary cleaning and treatment zones, with only the most essential zones being shown here for reasons of clarity. These are in particular a main cleaning stage 2, in which the containers, in particular returnable containers for beverage sales, are subjected to a main cleaning.
  • the main cleaning is carried out by means of a treatment liquid, in particular a main liquor, with a temperature of z. B. 80 ° C.
  • the liquor may be contacted with the containers as a dip or in some other form.
  • the main purification stage 2 is preceded by one or more pre-treatment stages 3, in which the containers are pretreated by treatment liquid, such as for example also an alkali or simple water, again in any suitable form, such as dipping or spraying or overflowing or the like the containers are preheated for treatment in the main cleaning stage 2, so that thermal stresses can be avoided, which lead to increased glass breakage, for example in glass containers, and the pretreatment result is improved.
  • treatment liquid such as for example also an alkali or simple water
  • two pre-treatment stages 3 are provided, namely a pre-soak 3a and a pre-leaching stage 3b.
  • the operating temperatures of the two pretreatment stages 3 are lower than in the main treatment stage 2 and are for example in the pretreatment stage 3a at about 40 ° C and in the pretreatment stage 3b at about 65 ° C.
  • the container cleaning system 1 further includes a cogeneration unit 4 of conventional construction, which provides at least the heat energy for the operation of the container cleaning and optionally also supplies the system with electrical power.
  • the cogeneration unit 4 is connected for this purpose via a heat circuit 5 with flow and return 5a, 5b with the container cleaning system 1. In the heat cycle 5, water with a temperature of z. B. 90 ° C fed.
  • the main purification stage 2 is connected via a heat exchanger 6 to the flow 5 a of the heat cycle 5.
  • the heat exchanger 6 may be of any construction and is connected to the main purification stage 2 via a pump 7 and a circulation line 7a.
  • the pump 7 conveys the treatment liquid of the main purification stage 2 from the treatment area through the heat exchanger 6 and back into the treatment area.
  • the heat medium of the heat cycle 5 is characterized on z. B. 83 ° C, this temperature reduction is too low to be effectively processed by the cogeneration unit 4.
  • a further heat exchanger 8 is turned on, which acts as a return cooler for the heat transfer medium in the heat cycle 5.
  • the coolant used are the cooler treatment liquids in the pretreatment stage 3, in particular the treatment liquid of the pre-soak in the pretreatment stage 3 b, which is slightly cooler at about 65 ° C. than the return 5 b from the first heat exchanger 6.
  • the heat exchanger 8 is also connected via a pump 9 and a circulation line 9a connected to the pretreatment stage 3b.
  • the return of the heat transfer medium from the heat cycle 5 can be cooled to a range between 68 ° C to 88 ° C, especially about 70 ° C, this represents the flow temperature of 90 ° C a sufficient temperature difference, as he from the cogeneration 4 can be processed better.
  • the second heat exchanger 8 is preferably coupled to a bypass line 10, through which the return from the first heat exchanger 6, the second heat exchanger 8 can bypass when the return from the first heat exchanger 6, for example when heating the main cleaning stage 2, has already been sufficiently cooled to operate the cogeneration unit 4 economically.
  • the pump 9 is controlled depending on the return temperature from the first heat exchanger 6, so that the cooling effect exerted by the second heat exchanger 8 on the heat transfer medium in the heat cycle 5, the temperature conditions and the heat demand of Main cleaning stage 2 can be adjusted to always return the cogeneration plant heat transfer medium, which is located in an economically operable by the power plant temperature range.
  • An exemplary container cleaning system is z. B. operated as follows.
  • the first pretreatment stage 3a is operated at about 40 ° and the second pretreatment stage 3b, the preheating at about 65 °, wherein in the second pretreatment stage 3b are 10.3 m 3 Vormérmlauge.
  • the main cleaning takes place at 80 ° C, whereby in the main cleaning stage 56, 24 m 3 lye are.
  • container 308 kW of heat energy in the pre-leaching stage 3b for example, from the pre-softening 3a deported and from this a heat energy amount of 171 kW is dragged into the main cleaning.
  • the heat transfer medium fed into the heating circuit 5 by the combined heat and power unit 4 has 90 ° C. and is provided at 21 to 24 m 3 / h and leaves the heating circuit 5 at 68 to 88 ° C. (mean value 70.5 ° C.).
  • the heat transfer medium is cooled to 83 ° C.
  • the pump capacities of the pumps 7 and 9 are 80 m 3 / h.
  • the values given may vary considerably depending on the type of machine or the type of container to be cleaned.
  • the temperature of the cleaning fluid may be between 58 and 85 ° C.
  • both pretreatment stages can be used as a recooler.
  • the temperature ranges can be adjusted to the corresponding and required operating temperatures of the main purification stage or pretreatment stage (s).
  • the above temperatures may vary, depending on the type of cogeneration plant used or the set temperatures in the cleaning system.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Cleaning By Liquid Or Steam (AREA)
  • Cleaning In General (AREA)

Claims (2)

  1. Installation de nettoyage de contenants ou récipients (1) comprenant au moins un étage de nettoyage principal (2) et au moins un étage de traitement préalable (3), qui travaillent chacun avec des liquides de traitement échauffés, l'étage de nettoyage principal (2) et l'étage de traitement préalable (3), pour leur alimentation en énergie calorifique, étant raccordés en commun à une centrale de cogénération (4), par l'intermédiaire d'un circuit de chauffage (5) commun, avec un circuit d'écoulement aller et retour (5a, 5b), l'étage de traitement préalable (3) étant raccordé dans le circuit d'écoulement de retour (5b), après l'étage de nettoyage principal (2), et
    l'installation de nettoyage de contenants comprenant, par ailleurs, un premier échangeur de chaleur (6) pour alimenter l'étage de nettoyage principal (2) en énergie calorifique,
    et un deuxième échangeur de chaleur (8) destiné à alimenter l'étage de traitement préalable (3) en énergie calorifique, monté en aval du premier échangeur de chaleur (6), et
    conçu pour un abaissement de température prédéterminé du fluide caloporteur dans le circuit de chauffage (5).
  2. Installation de nettoyage de contenants selon la revendication 1, dans laquelle il est prévu dans le circuit de chauffage (5), une conduite de dérivation (10) contournant l'échangeur de chaleur (8) de l'étage de traitement préalable (3).
EP11194229.8A 2011-01-14 2011-12-19 Installation de nettoyage de récipient Active EP2476492B1 (fr)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE102011002721.1A DE102011002721B4 (de) 2011-01-14 2011-01-14 Behälterreinigungsanlage

Publications (2)

Publication Number Publication Date
EP2476492A1 EP2476492A1 (fr) 2012-07-18
EP2476492B1 true EP2476492B1 (fr) 2014-02-26

Family

ID=45442878

Family Applications (1)

Application Number Title Priority Date Filing Date
EP11194229.8A Active EP2476492B1 (fr) 2011-01-14 2011-12-19 Installation de nettoyage de récipient

Country Status (3)

Country Link
EP (1) EP2476492B1 (fr)
CN (1) CN102580966B (fr)
DE (1) DE102011002721B4 (fr)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107838152B (zh) * 2017-11-03 2019-09-13 陈林余 一种水果深加工用水果罐头清洗装置

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3003663A1 (de) * 1980-02-01 1981-08-06 Holstein Und Kappert Gmbh, 4600 Dortmund Verfahren und vorrichtung zur reduzierung des durch umlaufende gefaesstraeger auftretenden waermeverlustes
DE3118647A1 (de) * 1981-05-11 1982-11-25 Holstein Und Kappert Gmbh, 4600 Dortmund Vorrichtung zum reinigen von flaschen
DE3205956A1 (de) 1982-02-19 1983-09-15 Robert 6141 Einhausen Becker Vorrichtung zur flaschenreinigung, bei der waerme zurueckgewonnen und frischwasser eingespart wird
EP0160775B1 (fr) * 1984-05-07 1989-01-11 Jacob Weitman Méthode de contrôle d'un système de récupération d'énergie
DD247436A1 (de) * 1986-03-31 1987-07-08 Ingbuero Und Rationalisierung Verfahren zur nutzung der abwaermeenergie von flaschenreinigungsmaschinen bei der warmabfuellung
DE10320078A1 (de) * 2003-05-05 2004-12-02 Krones Ag Vorrichtung zum Behandeln von Gegenständen mit Flüssigkeit
EP1705242A1 (fr) * 2005-03-23 2006-09-27 KRONES Aktiengesellschaft Installation de brasserie et procédé de brassage
DE102007059890A1 (de) * 2007-12-12 2009-06-25 Kulmbacher Brauerei Ag Vorrichtung und Verfahren zum Reinigen von Flaschen
DE202008014330U1 (de) 2008-10-28 2009-01-22 Kaspar Schulz Brauereimaschinenfabrik & Apparatebauanstalt Kg Vorrichtung zur Energieversorgung einer Brauerei
DE102009013579A1 (de) * 2009-03-19 2010-09-23 Gea Brewery Systems Gmbh Brauereianlage zur Herstellung und Abfüllung von Bier

Also Published As

Publication number Publication date
EP2476492A1 (fr) 2012-07-18
DE102011002721B4 (de) 2023-03-23
CN102580966B (zh) 2015-04-01
CN102580966A (zh) 2012-07-18
DE102011002721A1 (de) 2012-07-19

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