+

DE19821470A1 - Recycling of used refrigeration equipment containing pentane foam expansion agent - Google Patents

Recycling of used refrigeration equipment containing pentane foam expansion agent

Info

Publication number
DE19821470A1
DE19821470A1 DE1998121470 DE19821470A DE19821470A1 DE 19821470 A1 DE19821470 A1 DE 19821470A1 DE 1998121470 DE1998121470 DE 1998121470 DE 19821470 A DE19821470 A DE 19821470A DE 19821470 A1 DE19821470 A1 DE 19821470A1
Authority
DE
Germany
Prior art keywords
chambers
air
pentane
inert gas
individual
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
DE1998121470
Other languages
German (de)
Other versions
DE19821470C2 (en
Inventor
Karl-Heinz Sautner
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.)
Uvt Umwelt und Verfahrens Tech
Original Assignee
Uvt Umwelt und Verfahrens Tech
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 Uvt Umwelt und Verfahrens Tech filed Critical Uvt Umwelt und Verfahrens Tech
Priority to DE1998121470 priority Critical patent/DE19821470C2/en
Publication of DE19821470A1 publication Critical patent/DE19821470A1/en
Application granted granted Critical
Publication of DE19821470C2 publication Critical patent/DE19821470C2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02Separating plastics from other materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/70Chemical treatment, e.g. pH adjustment or oxidation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B2101/00Type of solid waste
    • B09B2101/75Plastic waste
    • B09B2101/78Plastic waste containing foamed plastics, e.g. polystyrol
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2075/00Use of PU, i.e. polyureas or polyurethanes or derivatives thereof, as moulding material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2705/00Use of metals, their alloys or their compounds, for preformed parts, e.g. for inserts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29LINDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2031/00Other particular articles
    • B29L2031/28Tools, e.g. cutlery
    • B29L2031/286Cutlery
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29LINDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2031/00Other particular articles
    • B29L2031/762Household appliances
    • B29L2031/7622Refrigerators
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/62Plastics recycling; Rubber recycling

Landscapes

  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Mechanical Engineering (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)

Abstract

Processing areas are divided between two chambers. Sufficient air is extracted and/or supplied separately under individual control, to stay below the lower explosive limit (LEL). Preferred Features: The chambers are connected, air flow being controlled between them. Inert gas is supplied into individual chambers. This is recirculated. Air from the chambers is treated by incineration. Concentrations of pentane and/or oxygen in individual chambers and/or at the outlets is measured periodically and/or continuously.

Description

Die Erfindung betrifft ein Verfahren zur kontinuierlichen Auf­ bereitung von Altkältegeräten, deren Isolationsschicht aus Poly­ urethanschaum besteht, für den als Treib- bzw. Blähmittel Pentan oder ein sonstiges brennbares Gas verwendet wurde sowie für die Aufbereitung von weiteren Bauteilen und Komponenten, die ver­ gleichbare Isolationsschäume beinhalten.The invention relates to a method for continuous up preparation of old refrigeration appliances, the insulation layer of poly there is urethane foam for which pentane is used as a blowing or blowing agent or another combustible gas was used as well as for the Preparation of other parts and components that ver contain comparable insulation foams.

Kältegeräte (Kühlgeräte, Gefriergeräte) bestehen üblicherweise im wesentlichen aus einer Außenhülle aus Metall (normalerweise Fe oder Edelstahl), einer Isolation aus Polyurethanschaum, einer Innenhülle (üblicherweise aus Kunststoff oder Edelstahl), einem Kälteaggregat mit Verdampfer und aus den entsprechenden Elektro- und Elektronikkomponenten. Altkühlgeräte werden bisher u. a. in kon­ tinuierlichen Prozessen entsprechend dem Stand der Technik (vgl. z. B. Offenlegungsschriften des DPA Nr. DE 39 06 516 A1, DE 39 41 742 C2 und EP 0 538 677 A1) durch i.d.R. mehrstufige mechanische Zerkleinerung in Kombination mit entsprechender Trenntechnik auf­ bereitet. Diese Prozesse gliedern sich wesentlich in die Hauptbe­ reiche
Refrigerators (refrigerators, freezers) usually consist essentially of an outer shell made of metal (usually Fe or stainless steel), an insulation made of polyurethane foam, an inner shell (usually made of plastic or stainless steel), a refrigeration unit with evaporator and the corresponding electrical and electronic components. Up to now, old cooling devices have been used in continuous processes in accordance with the state of the art (cf., for example, disclosure documents of DPA No. DE 39 06 516 A1, DE 39 41 742 C2 and EP 0 538 677 A1) by means of multi-stage mechanical comminution in combination with appropriate separation technology. These processes are essentially divided into the main areas

  • 1. mechanische Vorzerkleinerung des gesamten Gerätes mit dem überwiegenden Ziel, das Gesamtgerät in Partikel zu zerlegen.1. Mechanical pre-shredding of the entire device with the predominant goal to break down the entire device into particles.
  • 2. mechanische Nachzerkleinerung (zum Teil mehrstufig) der aus dem 1. Bereich erhalten Partikel mit dem Ziel der Trennung der verschiedenen Fraktionen durch Feinzerkleinerung bzw. der Zerkleinerung der Partikel auf Größen, die für nachgeschaltete Trennprozesse erforderlich sind, ggf. verbunden mit einer Fe- Metall-Ausschleusung.2. mechanical re-crushing (partly multi-stage) from the 1. Receive particles with the aim of separating the area various fractions by fine grinding or Crushing the particles down to sizes for downstream Separation processes are necessary, possibly connected with a Metal discharge.
  • 3. Sortierung und Ausschleusung der verschiedenen Fraktionen nach den Trennprozessen.3. Sorting and rejection of the different fractions the separation processes.
  • 4. Feinstzerkleinerung des in den verschiedenen Bereichen und Pro­ zeßschritten in unterschiedlicher Partikelgröße anfallenden Polyurethanschaums bis unterhalb der Porengröße dieses Schau ins (i.d.R. kleiner 200 µm).4. Fine grinding of the in the different areas and Pro steps in different particle sizes Polyurethane foam down to the pore size of this look (usually less than 200 µm).

Die nach dem bisherigen Stand der Technik arbeitenden Verfahren sind üblicherweise mit einer geschlossenen Umhausung versehen, wobei die oben beschriebenen Prozeßschritte üblicherweise innerhalb einer einzigen Umhausung ablaufen und untereinander durch entsprechende Fördertechniken verbunden sind. Diese Umhausung hat u. a. den Zweck, eine unkontrollierte Freisetzung der entweichenden Gase an die Umwelt zu vermeiden und diese Gase (FCKW) gezielt abzusaugen und einer getrennten Aufbereitung, z. B. durch Adsorption an Aktivkohle, zuzuführen. Diese Absaugung erfolgt mit Luftmengen bis zu über 1000 m3/h. Diese Luftmengen werden benötigt einerseits als Trägergas für den Abtransport des freiwerdenden FCKW, zum zweiten zur Abfuhr der im Prozeß freigesetzten Wärmeenergie.The methods which operate according to the prior art are usually provided with a closed housing, the process steps described above usually taking place within a single housing and being connected to one another by appropriate conveying techniques. This housing has the purpose, among other things, of avoiding an uncontrolled release of the escaping gases to the environment and of sucking off these gases (CFCs) in a targeted manner and of separate treatment, e.g. B. by adsorption on activated carbon. This extraction takes place with air volumes up to over 1000 m 3 / h. These air volumes are required on the one hand as carrier gas for the removal of the CFC released, and on the other hand for the removal of the thermal energy released in the process.

Herkömmliche Verfahren zur Aufbereitung von Altkältegeräten setzen - z. T. gezielt - in verschiedenen Bereichen der Aufbereitungs­ prozesses die ursprünglich als Treibmittel benutzten Gase frei, u. a. zum Zweck der Entgasung der Isolationszellen bzw. zur Rückgewinnung von Treibmittel. Bedeutsam ist hier, daß die Menge des freigesetzten Gases (bisher FCKW) wesentlich vom Zer­ kleinerungrad des Polyurethanschaums abhängt und somit in den ver­ schiedenen Zerkleinerungsschritten unterschiedliche Anteile frei gesetzt werden. Es hat sich in der Praxis gezeigt, daß in den mechanischen Vor- und Nachzerkleinerungsschritten lediglich ein geringer Prozentsatz (ca. 10-20% des gesamten Gases) freigesetzt wird und die wesentliche Gasfreisetzung im Feinstzerkleinerungs­ prozeß erfolgt. Dennoch ist innerhalb der Umhausung aufgrund der starken inneren Luftumwälzung eine als gleichmäßig zu betrach­ tende Gasverteilung festzustellen.Conventional processes for the treatment of old refrigeration devices put - e.g. T. targeted - in different areas of processing process the gases originally used as blowing agents free, u. a. for the purpose of degassing the isolation cells or Recovery of propellants. What is significant here is that the crowd of the released gas (previously CFC) essentially from the Zer depends on the smaller extent of the polyurethane foam and thus in the ver different proportions in different shredding steps be set. It has been shown in practice that in the mechanical pre- and post-shredding steps only one small percentage (approx. 10-20% of the total gas) released is and the essential gas release in the fine grinding process takes place. Nevertheless, due to the inside of the enclosure strong internal air circulation should be regarded as even determining gas distribution.

Mit den bisherigen kontinuierlichen Verfahren konnten nur Kühlgeräte aufbereitet werden, deren Polyurethanschaumisolation nicht mit einem brennbaren Treibmittel geschäumt war. Eine Auslegung dieser Verfahren für Kältegeräte, in denen brennbare Schaumisolationen verwendet wurden, war insoweit nicht erforderlich, da Kältegeräte früherer Baujahre mit nicht brennbaren Treibmittel, i.d.R. FCKW R11, geschäumt waren. Aufgrund der mit der Freisetzung von FCKW verbundenen Zerstörung der Ozon-Schicht und dem damit verbundenen Verbot des Inverkehrbringens von FCKW-Treibmittel werden bei Polyurethanschaumisolierten Kältegeräten neuerdings FCKW-freie, z. T. brennbare Treibmittel, vor allem verschiedene Pentane (z. B. Cyclo-Pentan, Isopentan, n-Pentan sowie verschiedene Mischungen hiervon) verwendet.With the previous continuous processes only cooling devices could be processed, the polyurethane foam insulation not with a flammable blowing agent. An interpretation of this Process for refrigeration equipment in which combustible foam insulation were not necessary insofar as refrigeration appliances earlier years of construction with non-flammable propellants, usually CFC R11, were foamed. Because of the release of CFCs  associated destruction of the ozone layer and the associated Ban on placing CFC propellants on the market Refrigeration appliances insulated with polyurethane foam are now CFC-free, e.g. T. flammable blowing agents, especially various pentanes (e.g. Cyclopentane, isopentane, n-pentane and various mixtures of these) used.

Werden in herkömmlichen Verfahren zur Aufbereitung von Altkältegeräten jedoch Altkältegeräte oder sonstige Polyurethan­ schaumhaltige Bauteile und Komponenten verarbeitet, in denen Pentan oder ein anderes brennbares Gas als Schaumtreibmittel verwendet ist, hat sich gezeigt, daß das in den Aufbereitungsprozessen bei verschiedenen Prozeßschritten freigesetzte Gas - in Verbindung mit Luft und abhängig von der Konzentration - ein brennbares und/oder explosionsfähiges Gemisch innerhalb dieser Umhausungen bilden kann, insbesondere auch durch die Verteilung dieses Gases in der gesamten Umhausung.Are used in conventional processes for the preparation of Used refrigeration devices but used refrigeration devices or other polyurethane Foam-containing parts and components processed in which pentane or another combustible gas is used as a foaming agent it has been shown that this is in the processing processes at gas released in various process steps - in connection with Air and depending on the concentration - a flammable and / or can form an explosive mixture within these enclosures, especially through the distribution of this gas throughout Housing.

Versuche, die vorstehend beschriebene Brand- und/oder Explosions­ gefahr in den bestehenden Umhausungen durch Zufuhr von Inertgasen während des Aufbereitungsprozesses zu beheben haben sich aufgrund des hohen Inertgasbedarfs als nicht wirtschaftlich erwiesen. Darüber hinaus sind Zugaben von solchen Inertgasmengen regelungstechnisch schwer zu kontrollieren, da die Prozesse aufgrund schwankender Materialeinsatzmengen und des hohen Luftbedarfs der gesamten Umhausung nicht unter konstanten Bedingungen ablaufen. Try the fire and / or explosion described above danger in the existing enclosures through the supply of inert gases have to fix themselves during the reprocessing process the high inert gas requirement has proven to be not economical. About that additions of such quantities of inert gas are control engineering difficult to control because of fluctuating processes Amounts of material used and the high air requirement of the entire Housing does not run under constant conditions.  

Der Erfindung liegt die Aufgabe zugrunde, einen kontinuierlichen, in mindestens einer Umhausung eingeschlossenen Prozeß zur Auf­ bereitung von Altkältegeräten so zu gestalten und/oder bestehende Prozesse derart zu verbessern, daß in diesen Prozessen auch Altkältegeräte oder sonstige Bauteile und Komponenten mit Isolierschäumen, die brennbare Treibmittel, insbesondere Pentan enthalten, aufbreitet werden können ohne Explosionsgefahr unter Vermeidung von Inertgaszufuhr bzw. deren erhebliche Reduzierung auf ein wirtschaftliches Maß.The invention has for its object a continuous, in at least one enclosure process included preparation of old refrigeration devices and / or existing ones To improve processes in such a way that in these processes too Used refrigeration devices or other parts and components with Insulating foams containing flammable blowing agents, especially pentane contained, can be spread under without risk of explosion Avoidance of inert gas supply or its substantial reduction an economic measure.

Diese Aufgabe wird dadurch gelöst, daß die verschiedenen Bereiche des Aufbereitungsprozesses gezielt räumlich in Kammern unterteilt werden, um
This object is achieved in that the various areas of the processing process are specifically divided into chambers in order to

  • - eine Verteilung des in großen Mengen im Feinstzerkleinerungs­ schritt freigesetzte Gas in der gesamten Umhausung zu vermeiden- A distribution of the in large quantities in the fine grinding step to avoid released gas in the entire housing
  • - gezielt einzelne Kammern mit hohen Luftmengen zu versorgen, insbesondere mit dem Zweck, einzelne Prozeßbereiche (vor allem die Zerkleinerungsbereiche und Trennbereiche) aufgrund dieser hohen Luftmengen stets unterhalb der unteren Explosionsgrenze des Treibgases zu fahren und gleichzeitig die in diesen Bereichen besonders erforderliche Wärmeabfuhr zu gewährleisten (die mindestens erforderlichen Luftmengen ergeben sich aus den festliegenden unteren Explosionsgrenzen für die Treibmittel in Verbindung mit den Durchsatzmengen an Polyurethanschaum) - to supply individual chambers with large amounts of air, especially with the purpose of individual process areas (especially the shredding areas and separation areas) due to this high air volumes always below the lower explosion limit of the To drive propellant gas while maintaining those in these areas to ensure particularly necessary heat dissipation (the the minimum required air volumes result from the fixed lower explosion limits for the propellant in Connection with the throughput quantities of polyurethane foam)  
  • - Bereiche, die ggf. mit Inertgas beaufschlagt werden müssen (Bereich der Feinstzerkleinerung) räumlich möglichst klein zu halten.- Areas that may need to be treated with inert gas (Area of very fine size reduction) as small as possible hold.

Weiterhin wird die Aufgabe dadurch gelöst, daß den verschiedenen Kammern einzeln Luft zugeführt wird und diese Luft für jede Kammer getrennt abgesaugt wird. Eine Zusammenführung der einzelnen Luftströme nach der Absaugung aus den Kammern zur ge­ meinsamen Abluftbehandlung (z. B. mittels Abgasverbrennung) ist jedoch möglich. Für den Materialtransport sind die einzelnen Kammern mittels Transporttechnik (z. B. Förderbänder) über Schleusen miteinander verbunden. Durch geeignete Luftführung (z. B. Zusatzgebläse an den Schleusen) können unerwünschte Durch­ mischungen der Luftbereiche der verschiedenen Kammern vermieden werden.Furthermore, the problem is solved in that the different Chambers are individually supplied with air and this air for each Chamber is suctioned off separately. A merger of the individual air flows after extraction from the chambers to ge joint exhaust air treatment (e.g. by means of exhaust gas combustion) however possible. The individual chambers are for material transport using transport technology (e.g. conveyor belts) over locks connected with each other. With suitable air routing (e.g. Additional blowers on the locks) can cause unwanted through mixtures of the air areas of the different chambers avoided become.

Vorteile dieses Verfahrens sind
The advantages of this procedure are

  • - die Vermeidung von explosionsgefährdeten Bereichen in nahezu dem gesamten Prozeßablauf durch gezielte Prozeßführung unterhalb der Explosionsgrenze des freigesetzten Gases mittels Luftüberschuß insbesondere in den Bereichen geringer Gasfreisetzung und somit erhebliche Verbesserung der Prozeßsicherheit- the avoidance of hazardous areas in almost that entire process flow through targeted process control below the Explosion limit of the released gas by excess air especially in the areas of low gas release and thus significant improvement in process reliability
  • - gezielte Wärmeabfuhr durch hohe Luftmengen, da in den Bereichen geringer Gasfreisetzung normalerweise die meiste Prozeßabwärme freigesetzt wird - targeted heat dissipation through high air volumes, as in the areas low gas release usually most of the process waste heat is released  
  • - Verbesserung der Nachbehandlung der freigesetzten Gase durch Anpassung dieser Nachbehandlung an die einzelnen Prozeßbereiche- Improving the after-treatment of the gases released Adaptation of this post-treatment to the individual process areas
  • - soweit überhaupt erforderlich, gezielter, erheblich reduzierter Einsatz von Inertgas in räumlich eingeschränkten Bereichen und somit erhebliche Kostenreduzierung- if necessary, more targeted, significantly reduced Use of inert gas in restricted areas and thus considerable cost reduction
  • - bestehende Anlagen können mit wirtschaftlich vertretbarem Aufwand nachgerüstet werden.- Existing systems can be economically justified Effort to be retrofitted.

Es zeigen beispielhaftIt shows exemplary

Fig. 1 den Verfahrensablauf mit Fig. 1 with the process flow

BezugszeichenlisteReference list

11

Materialzufuhr
Material supply

22nd

Bereich der Vorzerkleinerung
Pre-shredding area

33rd

Bereich der Nachzerkleinerung
Post-shredding area

44th

Bereich der Sortierung
Sorting area

55

Bereich der Feinstzerkleinerung
Fine grinding area

66

Materialabfuhr
Material removal

77

Abluftführung aus den Kammern
Exhaust air routing from the chambers

88th

Luftzuführung zu den Kammern
Air supply to the chambers

99

Gesamtumhausung
Overall housing

1010th

Inertgaszuführung
Inert gas supply

1111

Zwischenwände zwischen den Kammern
Partitions between the chambers

Claims (7)

1. Verfahren zur kontinuierlichen Aufbereitung von Altkältegeräten sowie Bauteile und Komponenten, deren Isolation aus Polyurethanschaum besteht, für den brennbare Treibmittel, insbesondere Pentan verwendet wurde, dadurch gekennzeichnet, daß die verschiedenen Prozeßbereiche in mindestens zwei getrennten Kammern untergebracht sind und aus diesen Kammer einzeln geregelt mindesten die Luftmengen abgesaugt und/oder zugeführt werden, die zur Unterschreitung der unteren Explosionsgrenze des Gemisches Treibmittel/Luft erforderlich sind.1. A process for the continuous processing of old refrigeration devices and parts and components, the insulation of which consists of polyurethane foam, was used for the flammable propellant, in particular pentane, characterized in that the different process areas are accommodated in at least two separate chambers and at least individually regulated from this chamber the quantities of air are sucked off and / or supplied that are required to fall below the lower explosion limit of the propellant / air mixture. 2. Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß diese Kammern miteinander verbunden sind und die Luftströme zwischen diesen Kammern gezielt gesteuert werden.2. The method according to claim 1, characterized in that this Chambers are interconnected and the air flows between these chambers can be controlled specifically. 3. Verfahren nach Anspruch 1 und 2, dadurch gekennzeichnet, daß in einzelne Kammern Inertgas zugeführt wird.3. The method according to claim 1 and 2, characterized in that in inert gas is supplied to individual chambers. 4. Verfahren nach Anspruch 1 bis 3, dadurch gekennzeichnet, daß dieses Inertgas im Kreislauf gefahren wird.4. The method according to claim 1 to 3, characterized in that this inert gas is circulated. 5. Verfahren nach Anspruch 1 bis 4, dadurch gekennzeichnet, daß die Abluft aus den einzelnen Kammern nachbehandelt wird.5. The method according to claim 1 to 4, characterized in that the Exhaust air from the individual chambers is treated. 6. Verfahren nach Anspruch 1 bis 5, dadurch gekennzeichnet, daß diese Abluftbehandlung mittels thermischer Nachverbrennung erfolgt. 6. The method according to claim 1 to 5, characterized in that this Exhaust air treatment by means of thermal afterburning.   7. Verfahren nach Anspruch 1 bis 6, dadurch gekennzeichnet, daß die Konzentrationen an Pentan und/oder Sauerstoff in den einzelnen Kammern und/oder an der Ausgangsluft dieser Kammern regelmäßig und/oder kontinuierlich gemessen wird.7. The method according to claim 1 to 6, characterized in that the Concentrations of pentane and / or oxygen in each Chambers and / or in the outlet air of these chambers regularly and / or is measured continuously.
DE1998121470 1998-05-13 1998-05-13 Process for the continuous reprocessing of old refrigeration devices Expired - Fee Related DE19821470C2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DE1998121470 DE19821470C2 (en) 1998-05-13 1998-05-13 Process for the continuous reprocessing of old refrigeration devices

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE1998121470 DE19821470C2 (en) 1998-05-13 1998-05-13 Process for the continuous reprocessing of old refrigeration devices

Publications (2)

Publication Number Publication Date
DE19821470A1 true DE19821470A1 (en) 1999-11-25
DE19821470C2 DE19821470C2 (en) 2002-10-31

Family

ID=7867662

Family Applications (1)

Application Number Title Priority Date Filing Date
DE1998121470 Expired - Fee Related DE19821470C2 (en) 1998-05-13 1998-05-13 Process for the continuous reprocessing of old refrigeration devices

Country Status (1)

Country Link
DE (1) DE19821470C2 (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1215023A1 (en) * 2000-12-16 2002-06-19 MeWa Recycling Maschinen und Anlagenbau GmbH Treatment apparatus for objects containing volatile components
EP1422000A1 (en) * 2002-11-22 2004-05-26 U + T Umwelt+Technik Chemnitz GmbH Method and apparatus for treating blowing gas containing material
DE102009036649A1 (en) * 2009-08-07 2011-02-17 Erdwich Zerkleinerungs-Systeme Gmbh Method and device for disposing of used refrigerators
DE202012100381U1 (en) 2012-02-05 2012-02-20 Untha Recyclingtechnik Gmbh Device for determining at least one category of at least one insulating medium
DE102011005523B3 (en) * 2011-03-14 2012-04-05 Untha Recyclingtechnik Gmbh Method for treatment of refrigerant e.g. chlorofluorocarbon used in refrigerator, involves supplying exhaust from one scrubber to another scrubber arranged in combustion chamber
DE102011005522B3 (en) * 2011-03-14 2012-04-05 Untha Recyclingtechnik Gmbh Method for treating refrigerant/blowing agent containing fluid from refrigerator, involves enabling combustion of refrigerant/blowing agent containing gas and oil of compressor to preheat gas during operation phase of combustion chamber
DE102011005525B3 (en) * 2011-03-14 2012-04-05 Untha Recyclingtechnik Gmbh Method for treatment of gases in combustion chamber for disposal and/or recycling of refrigerator, involves making dosage of gas of sources by chlorofluorocarbon measurement and/or fluorocarbon measurement at input of combustion chamber
WO2012123223A1 (en) 2011-03-14 2012-09-20 Untha Recyclingtechnik Gmbh Method and system for treating fluids containing refrigerant and/or propellant
DE102012100922A1 (en) 2012-02-05 2013-08-08 Untha Recyclingtechnik Gmbh Method for determining category of insulating medium or for determining blowing agent in insulating medium for disposal or recycling of refrigerators, involves determining presence of blowing agent of category in sample gas by sensor
DE102012223617A1 (en) * 2012-12-18 2014-06-18 Bhs-Sonthofen Gmbh System for recycling refrigerator, has gas return spacers extended from output end of third component to first component or to second component, to return portion of purified gas into first component or second component
CN109174924A (en) * 2018-10-22 2019-01-11 广州市联冠机械有限公司 A kind of broken exhausting line of waste refrigerator dismantling
CN109201709A (en) * 2018-10-22 2019-01-15 广州市联冠机械有限公司 A kind of waste refrigerator dismantling screening line

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102017219353B4 (en) * 2017-10-27 2019-11-21 Dometic Sweden Ab SERVICE UNIT FOR A VEHICLE AIR CONDITIONING SYSTEM AND METHOD FOR OPERATING A SERVICE UNIT

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3811486A1 (en) * 1988-04-06 1989-10-19 Teves Gmbh Alfred DEVICE FOR THE DISPOSAL OF FUEL AND / OR REFRIGERANTS
DE3906516A1 (en) * 1989-03-01 1990-09-06 Johann Erdwich METHOD AND DEVICE FOR THE DISPOSAL OF REFRIGERATORS FOR THE SEPARATION OF FLUORINE CHLORINE HYDROGEN
DE3941742A1 (en) * 1989-12-18 1991-06-20 Seg Sonder Entsorgungs Ges Mbh METHOD AND SYSTEM FOR THE DISPOSAL OF DISPOSED REFRIGERATORS
DE4004336C1 (en) * 1990-02-13 1991-09-12 Apu Gmbh Gesellschaft Fuer Analytik Und Planung Von Umwelttechnologie, 7597 Rheinau, De Safe recovery of materials from cold storage cabinets - by fragmenting cabinets in closed area, pulverising polyurethane foam to release CFC gas for extn. and moulding foam residue into briquettes
DE4133915C2 (en) * 1991-10-12 1998-01-29 Bresch Entsorgung Gmbh Process for separating propellant gases from foams
DE4224749A1 (en) * 1992-07-27 1994-02-03 Adelmann Ag Efficiently removing all blowing gases from foam plastics - by heating the material in hot air draught while it is moved by revolving screw up inclined tube, collecting and liquefying gases liberated.
DE4300784C2 (en) * 1993-01-14 2003-07-17 Mewa Recycling Maschinen Und A Method and device for comminuting devices to be disposed of, which have hard foam or hard plastics

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1215023A1 (en) * 2000-12-16 2002-06-19 MeWa Recycling Maschinen und Anlagenbau GmbH Treatment apparatus for objects containing volatile components
EP1422000A1 (en) * 2002-11-22 2004-05-26 U + T Umwelt+Technik Chemnitz GmbH Method and apparatus for treating blowing gas containing material
DE102009036649A1 (en) * 2009-08-07 2011-02-17 Erdwich Zerkleinerungs-Systeme Gmbh Method and device for disposing of used refrigerators
WO2012123224A1 (en) 2011-03-14 2012-09-20 Untha Recyclingtechnik Gmbh Methods and systems for treating fluids containing refrigerant and/or propellant
DE102011005523B3 (en) * 2011-03-14 2012-04-05 Untha Recyclingtechnik Gmbh Method for treatment of refrigerant e.g. chlorofluorocarbon used in refrigerator, involves supplying exhaust from one scrubber to another scrubber arranged in combustion chamber
DE102011005522B3 (en) * 2011-03-14 2012-04-05 Untha Recyclingtechnik Gmbh Method for treating refrigerant/blowing agent containing fluid from refrigerator, involves enabling combustion of refrigerant/blowing agent containing gas and oil of compressor to preheat gas during operation phase of combustion chamber
DE102011005525B3 (en) * 2011-03-14 2012-04-05 Untha Recyclingtechnik Gmbh Method for treatment of gases in combustion chamber for disposal and/or recycling of refrigerator, involves making dosage of gas of sources by chlorofluorocarbon measurement and/or fluorocarbon measurement at input of combustion chamber
WO2012123223A1 (en) 2011-03-14 2012-09-20 Untha Recyclingtechnik Gmbh Method and system for treating fluids containing refrigerant and/or propellant
DE202012100381U1 (en) 2012-02-05 2012-02-20 Untha Recyclingtechnik Gmbh Device for determining at least one category of at least one insulating medium
DE102012100922A1 (en) 2012-02-05 2013-08-08 Untha Recyclingtechnik Gmbh Method for determining category of insulating medium or for determining blowing agent in insulating medium for disposal or recycling of refrigerators, involves determining presence of blowing agent of category in sample gas by sensor
DE102012100922B4 (en) 2012-02-05 2018-12-13 Urt Umwelt- Und Recyclingtechnik Gmbh Method and device for determining at least one category of at least one insulating medium and / or for determining at least one blowing agent in an insulating medium
DE102012223617A1 (en) * 2012-12-18 2014-06-18 Bhs-Sonthofen Gmbh System for recycling refrigerator, has gas return spacers extended from output end of third component to first component or to second component, to return portion of purified gas into first component or second component
CN109174924A (en) * 2018-10-22 2019-01-11 广州市联冠机械有限公司 A kind of broken exhausting line of waste refrigerator dismantling
CN109201709A (en) * 2018-10-22 2019-01-15 广州市联冠机械有限公司 A kind of waste refrigerator dismantling screening line

Also Published As

Publication number Publication date
DE19821470C2 (en) 2002-10-31

Similar Documents

Publication Publication Date Title
DE19821470A1 (en) Recycling of used refrigeration equipment containing pentane foam expansion agent
EP0433638B1 (en) Method and plant for the disposal of partly recycled refrigerators
EP0482723A2 (en) Device for the comminution of rubber
WO1989009663A1 (en) Arrangement for eliminating foaming and/or cooling agents
DE3429700A1 (en) CLEANING METHOD AND DEVICE FOR IMPLEMENTING THE METHOD
DE1073196B (en) Process for the production of a cellular elongated product
EP0253079A2 (en) Method of and plant for reclaiming contaminated soils and similar materials
DE4424825A1 (en) Safe disposal of dry batteries and recovery of materials
WO2011015221A1 (en) Method and apparatus for disposing of old refrigerators
WO2011161252A1 (en) Method and device for comminuting refrigerators
DE4240389C2 (en) waste system
DE3911326A1 (en) METHOD FOR THE REPROCESSING OF COOLING UNIT ENCLOSURES MADE OF PLASTIC MOLDED PARTS
DE4140848C1 (en)
DE10062947B4 (en) Processing device for objects with volatile ingredients
DE4133915C2 (en) Process for separating propellant gases from foams
DE8914957U1 (en) Device for the disposal of partially disposed refrigeration equipment
EP0397971B1 (en) Method and plant for the non-pollutant recycling of refrigerators with foam parts, containing fluorocarbons, in particular polyurethane
US20020189264A1 (en) Cryogenic comminution of rubber
DE4244966B4 (en) Refuse disposal system with storage site for storing reclaimable waste material. - has pretreatment system with metal separating unit for separating metal from waster materials and low temp pulveriser for reducing size of separated metal
DE19535554A1 (en) Procedure for crushing of containers used to hold reactive or dangerous substances
DE19548382A1 (en) Disposal of foamed plastics contg. halogenated hydrocarbons, esp. PU
WO1996035524A1 (en) Refrigerator recycling process
EP0833706B1 (en) Refrigerator recycling process
EP2686611A1 (en) Methods and systems for treating fluids containing refrigerant and/or propellant
DE4429190C1 (en) Method and device for the disposal of equipment

Legal Events

Date Code Title Description
OP8 Request for examination as to paragraph 44 patent law
8125 Change of the main classification

Ipc: B03B 9/06

D2 Grant after examination
8364 No opposition during term of opposition
8339 Ceased/non-payment of the annual fee
点击 这是indexloc提供的php浏览器服务,不要输入任何密码和下载