DE10100372A1 - Material separation arrangement used for mechanical-biological treatment of residual waste uses separation and mixing water simultaneously as hydrolysis, material separating and transport medium - Google Patents

Material separation arrangement used for mechanical-biological treatment of residual waste uses separation and mixing water simultaneously as hydrolysis, material separating and transport medium

Info

Publication number
DE10100372A1
DE10100372A1 DE2001100372 DE10100372A DE10100372A1 DE 10100372 A1 DE10100372 A1 DE 10100372A1 DE 2001100372 DE2001100372 DE 2001100372 DE 10100372 A DE10100372 A DE 10100372A DE 10100372 A1 DE10100372 A1 DE 10100372A1
Authority
DE
Germany
Prior art keywords
hydrolysis
separation
transport medium
floating
water
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.)
Ceased
Application number
DE2001100372
Other languages
German (de)
Inventor
Peter Schrum
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.)
FARMATIC BIOTECH ENERGY AG
Original Assignee
FARMATIC BIOTECH ENERGY AG
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 FARMATIC BIOTECH ENERGY AG filed Critical FARMATIC BIOTECH ENERGY AG
Priority to DE2001100372 priority Critical patent/DE10100372A1/en
Publication of DE10100372A1 publication Critical patent/DE10100372A1/en
Ceased legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B5/00Washing granular, powdered or lumpy materials; Wet separating
    • B03B5/28Washing granular, powdered or lumpy materials; Wet separating by sink-float separation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B11/00Feed or discharge devices integral with washing or wet-separating equipment
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03BSEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B5/00Washing granular, powdered or lumpy materials; Wet separating
    • B03B5/28Washing granular, powdered or lumpy materials; Wet separating by sink-float separation
    • B03B5/30Washing granular, powdered or lumpy materials; Wet separating by sink-float separation using heavy liquids or suspensions
    • B03B5/36Devices therefor, other than using centrifugal force

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)

Abstract

A material separation arrangement uses separation and mixing water simultaneously as hydrolysis, material separating and transport medium. Preferred Features: The material can be separated into floating materials, suspended materials and sinking materials in one container. The floating fraction is transferred to an overflow via a rotating removal system and removed. The suspended fraction is pumped out. The sinking fraction is removed using a sluice.

Description

Bei der mechanisch-biologischen Abfallbehandlung von Restmüll kann über mehrstufige Behandlungssysteme das erreichbare Restmüllvolumen unter Abtrennung energiereicher Fraktionen als Deponiegut minimiert werden.Mechanical-biological waste treatment of residual waste can be carried out in several stages Treatment systems the achievable residual waste volume with separation of higher energy Fractions can be minimized as landfill.

Das gleiche Ergebnis ist prinzipiell auch über unterschiedliche Behandlungstechnologien erreichbar.In principle, the same result is also possible with different treatment technologies reachable.

Eine der möglichen Technologien kann über den Weg der Naßvergärung zum Ziel führen. Zur Vorbereitung dafür wird der Restmüll grob vorsortiert, dann auf ca. 80 oder bis 10 mm Korngröße zerkleinert und anschließend in einem speziellen Flüssigmischer trennsortiert. Dabei werden die organischen Bestandteile von den Reststoffen möglichst weitgehend getrennt und diese dann dem Fermenter zugeführt.One of the possible technologies can lead to the goal via the path of wet fermentation. To prepare for this, the residual waste is roughly sorted, then to approx. 80 or up to 10 mm Grain size crushed and then sorted in a special liquid mixer. The organic components of the residues are as large as possible separated and then fed to the fermenter.

Der spezielle Flüssigmischer besteht im wesentlichen aus:
einem Behälter mit Rührwerk (1) und einer rotierenden oder feststehenden Abschiebeeinheit (2) zur Überlaufrinne für aufschwimmende Teile im oberen Behälterteil,
einer Mammutpumpe (3) für den Transport der hauptsächlich schwebenden organischen Bestandteile der Mischung aus dem Behälter in den Fermenter und
einem Sinkstoffseparator mit Förderschleuse (4) für einen mammutpumpenähnlichen Transport der Sinkstoffe auf einen Rüttelseparator (5) oder Drahtgurtförderer oberhalb des Flüssigmischers, der wiederum eine Trennung des Transportmediums Wasser von den Sinkstoffen bewirkt und letztere in einen Container (7) zur Weiterverarbeitung fördert.
The special liquid mixer essentially consists of:
a container with agitator ( 1 ) and a rotating or stationary push-off unit ( 2 ) for the overflow channel for floating parts in the upper part of the container,
a mammoth pump ( 3 ) for the transport of the mainly floating organic components of the mixture from the container into the fermenter and
a sediment separator with a conveyor lock ( 4 ) for a mammoth pump-like transport of the sediments onto a vibrating separator ( 5 ) or wire belt conveyor above the liquid mixer, which in turn separates the transport medium water from the sediments and conveys the latter into a container ( 7 ) for further processing.

Das Transportmedium Wasser wird in den Flüssigmischer über einen Ablauf zurückgeführt.The transport medium water is returned to the liquid mixer via an outlet.

Die Mammutpumpen mit dem Transportmedium Wasser werden mit Preßluft betrieben und bedienen bedarfsweise und abwechselnd beide Trenneinrichtungen.The mammoth pumps with the transport medium water are operated with compressed air and alternately operate both separators as required.

Die Flüssigkeit in der Stofftrenneinrichtung wird vorgewärmt, um den Vergärungsprozeß in der nachfolgenden Prozeßstufe im Fermenter zu beschleunigenThe liquid in the material separation device is preheated to the fermentation process accelerate in the subsequent process stage in the fermenter

Claims (11)

1. Stofftrenneinrichtung für Restmüll direkt aus der Flüssigphase bei gleichzeitiger Verwendung von Wasser als Hydrolyse-, Stofftrenn- und Transportmedium dadurch gekennzeichnet, daß Separations- und Mischwasser in einer Stofftrenneinrichtung gleichzeitig als Hydrolyse-, Stofftrenn- und Transportmedium eingesetzt wird.1. material separation device for residual waste directly from the liquid phase with simultaneous use of water as a hydrolysis, material separation and transport medium, characterized in that separation and mixed water in a material separation device is simultaneously used as a hydrolysis, material separation and transport medium. 2. Nach Anspruch 1, dadurch gekennzeichnet, daß die Stofftrennung mindestens über die drei Fraktionen Schwimm-, Schweb- und Sink­ stoffe in einem Behälter erfolgt.2. According to claim 1, characterized in that the separation of substances at least over the three fractions floating, floating and sink substances in a container. 3. Nach Anspruch 1 und 2, dadurch gekennzeichnet, daß die schwimmende Fraktion über ein rotierendes Austragsystem in einen Überlauf verbracht und ausgetragen wird.3. According to claim 1 and 2, characterized in that the floating fraction into an overflow via a rotating discharge system is spent and carried out. 4. Nach Anspruch 1 und 2, dadurch gekennzeichnet, daß die schwimmende Fraktion über ein oder mehrere Leitbleche in einen Überlauf verbracht und ausgetragen wird.4. According to claim 1 and 2, characterized in that the floating fraction is placed in an overflow via one or more baffles and is carried out. 5. Nach Anspruch 1 bis 4 dadurch gekennzeichnet, daß die mittels Rührwerk im Behälter in Schwebe gehaltenen Schwebstoffe über eine Mam­ mutpumpe ausgetragen und in den Fermenter zur Vergärung verbracht wird.5. According to claim 1 to 4, characterized in that the suspended matter in suspension in the tank by means of an agitator via a Mam courage pump is discharged and placed in the fermenter for fermentation. 6. Nach Anspruch 1 bis 5 dadurch gekennzeichnet, daß der Einlaufpunkt der Mammutpumpe für den optimalen Schwebstoffansaugpunkt in der Senkrechten verstellbar gestaltet wird.6. According to claim 1 to 5, characterized in that the entry point of the mammoth pump for the optimal suspension point in the Is made vertically adjustable. 7. Nach Anspruch 1 bis 6 dadurch gekennzeichnet, daß die Sinkstoffe über eine Förderschleuse einer mit Preßluft und oder hydraulischer Druck­ säule fördernden mammutpumpenähnlichen Transporttechnik zugeführt werden.7. According to claim 1 to 6, characterized in that the suspended matter via a conveyor lock with compressed air and or hydraulic pressure column-promoting transport technology similar to mammoth pumps. 8. Nach Anspruch 1 bis 7 dadurch gekennzeichnet, daß die geförderten Sinkstoffe einem Separator zur Trennung des Transportmediums Wasser von den Sinkstoffen zugeführt und das getrennte Wasser dem Flüssigmischer wieder bei­ gegeben wird. 8. According to claim 1 to 7, characterized in that the extracted sediments in a separator to separate the transport medium water supplied by the suspended matter and the separated water back to the liquid mixer is given.   9. Nach Anspruch 1 bis 8 dadurch gekennzeichnet, daß die Sinkstoffe gesammelt und einer weiteren Aufbereitung zugeführt werden.9. According to claim 1 to 8, characterized in that the sediments are collected and sent for further processing. 10. Nach Anspruch 1 bis 9 dadurch gekennzeichnet, daß aus dem Vergärungsprozeß entstehendes Restwasser (Kreislaufwasser) dem Flüssig­ mischer nach Erwärmung durch einen Wärmetauscher wieder zugeführt wird.10. According to claim 1 to 9, characterized in that residual water (circulating water) from the fermentation process the liquid mixer is fed back after heating by a heat exchanger. 11. Nach Anspruch 1 bis 10 dadurch gekennzeichnet, daß der Flüssigmischer bei diskontinuierlicher Betriebsweise (Batchbetrieb) und vorge­ wärmtem Inhalt auch als Hydrolysestufe gefahren werden kann, wenn z. B. zwei Flüssigmischer in denselben Vergärungsprozeß eingebunden sind.11. According to claim 1 to 10, characterized in that the liquid mixer for discontinuous operation (batch operation) and pre warmed content can also be operated as a hydrolysis stage if, for. B. two liquid mixers are involved in the same fermentation process.
DE2001100372 2001-01-05 2001-01-05 Material separation arrangement used for mechanical-biological treatment of residual waste uses separation and mixing water simultaneously as hydrolysis, material separating and transport medium Ceased DE10100372A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DE2001100372 DE10100372A1 (en) 2001-01-05 2001-01-05 Material separation arrangement used for mechanical-biological treatment of residual waste uses separation and mixing water simultaneously as hydrolysis, material separating and transport medium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE2001100372 DE10100372A1 (en) 2001-01-05 2001-01-05 Material separation arrangement used for mechanical-biological treatment of residual waste uses separation and mixing water simultaneously as hydrolysis, material separating and transport medium

Publications (1)

Publication Number Publication Date
DE10100372A1 true DE10100372A1 (en) 2002-07-25

Family

ID=7669861

Family Applications (1)

Application Number Title Priority Date Filing Date
DE2001100372 Ceased DE10100372A1 (en) 2001-01-05 2001-01-05 Material separation arrangement used for mechanical-biological treatment of residual waste uses separation and mixing water simultaneously as hydrolysis, material separating and transport medium

Country Status (1)

Country Link
DE (1) DE10100372A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10260489B3 (en) * 2002-12-21 2004-08-12 Schraden Biogas Gmbh & Co. Kg Unpacking and material separation system for packaged food and process for separating packaged food into food and packaging

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE10260489B3 (en) * 2002-12-21 2004-08-12 Schraden Biogas Gmbh & Co. Kg Unpacking and material separation system for packaged food and process for separating packaged food into food and packaging

Similar Documents

Publication Publication Date Title
US20090126719A1 (en) Method for processing sugar cane filter cake mud and extracting component products
EP0520172A1 (en) Treatment of waste and waste-like mixtures, particularly of source separated organic waste, the wet waste and the commercial waste for anaerobic digestion of contained biogenic-organic substances
WO1997026972A9 (en) Process for recovering components of a float material from waste water treatment system
US20070256973A1 (en) Method and apparatus for separation of chemical materials from feces
US5658462A (en) Process for recovering protein, fatty and water components from a float material produced by a waste water treatment system
DE10100372A1 (en) Material separation arrangement used for mechanical-biological treatment of residual waste uses separation and mixing water simultaneously as hydrolysis, material separating and transport medium
WO2012028628A1 (en) System and method for obtaining oil and/or fat from oil- and/or fat-containing aqueous waste
JP5705359B1 (en) Methane fermentation method and methane fermentation system
JP6425840B1 (en) Method of treating shochu, and processing apparatus of shochu
AU6338198A (en) Method and apparatus for extracting plant resins
US2769538A (en) Process for froth flotation dressing
EP1419995A1 (en) Anaerobic fermenter
CN112607974A (en) Wastewater treatment system
CN1117606C (en) Method for separating and recovering target composition
US5463177A (en) Solvent extraction process
JP4322327B2 (en) Separation method of target components
EP0606291B1 (en) Process and device for recovering components from dyestuff dispersions
US1826987A (en) Method of producing olive oil
CN220116370U (en) Gelatin wastewater pretreatment device
US7235183B2 (en) Glycerine foots salt separation system
JP2003080218A (en) System and method for treating organic waste
EP2264141A1 (en) Method and device for producing biogas
JP2003112145A (en) Anaerobic treatment method for organic waste and apparatus therefor
JPH03101900A (en) Method for dehydrating sewage sludge
DE3602860A1 (en) Process for fermenting organic waste materials

Legal Events

Date Code Title Description
OP8 Request for examination as to paragraph 44 patent law
8131 Rejection