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DE20014110U1 - Plant for the treatment and disposal of waste - Google Patents

Plant for the treatment and disposal of waste

Info

Publication number
DE20014110U1
DE20014110U1 DE20014110U DE20014110U DE20014110U1 DE 20014110 U1 DE20014110 U1 DE 20014110U1 DE 20014110 U DE20014110 U DE 20014110U DE 20014110 U DE20014110 U DE 20014110U DE 20014110 U1 DE20014110 U1 DE 20014110U1
Authority
DE
Germany
Prior art keywords
plant
waste
fermenter
plant according
gasifier
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.)
Expired - Lifetime
Application number
DE20014110U
Other languages
German (de)
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.)
ROSINGER ENERGIEANLAGEN GmbH
Original Assignee
ROSINGER ENERGIEANLAGEN GmbH
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 ROSINGER ENERGIEANLAGEN GmbH filed Critical ROSINGER ENERGIEANLAGEN GmbH
Publication of DE20014110U1 publication Critical patent/DE20014110U1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B03—SEPARATION 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
    • B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
    • B03B9/00—General arrangement of separating plant, e.g. flow sheets
    • B03B9/06—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/02—Fixed-bed gasification of lump fuel
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0903—Feed preparation
    • C10J2300/0906—Physical processes, e.g. shredding, comminuting, chopping, sorting
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913—Carbonaceous raw material
    • C10J2300/0946—Waste, e.g. MSW, tires, glass, tar sand, peat, paper, lignite, oil shale
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953—Gasifying agents
    • C10J2300/0956—Air or oxygen enriched air
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0953—Gasifying agents
    • C10J2300/0973—Water
    • C10J2300/0976—Water as steam
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/16—Integration of gasification processes with another plant or parts within the plant
    • C10J2300/164—Integration of gasification processes with another plant or parts within the plant with conversion of synthesis gas
    • C10J2300/1643—Conversion of synthesis gas to energy
    • C10J2300/1646—Conversion of synthesis gas to energy integrated with a fuel cell
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00—Details of gasification processes
    • C10J2300/16—Integration of gasification processes with another plant or parts within the plant
    • C10J2300/1681—Integration of gasification processes with another plant or parts within the plant with biological plants, e.g. involving bacteria, algae, fungi
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Processing Of Solid Wastes (AREA)

Description

&ngr; &idigr;&iacgr;**··&idigr;&idigr;·#&bgr;.·&idigr;&iacgr;&iacgr;&idigr;&ngr;&idigr;&iacgr;**··&idigr;&idigr;·#&bgr;.·&idigr;&iacgr;&iacgr;&idigr;

WTE-ANLAGE ZUR ENERGETISCHEN VERWERTUNG VON BIOLOGISCH/ORGANISCH SYNTHETISCHEN FLÜSSIG-UND FESTSTOFFABFÄLLEN WTE PLANT FOR THE ENERGY RECYCLING OF BIOLOGICAL/ORGANIC SYNTHETIC LIQUID AND SOLID WASTE

BESCHREIBUNGDESCRIPTION

Die Entsorgung von Müll stellt weltweit ein großes Problem der.Waste disposal is a major problem worldwide.

Die Aufarbeitung erfolgt sehr kostenintensiv nach verschiedenen Verfahren, wobei nicht alle Stoffe umsetzbar sind . Deshalb fallen entsprechend große Mengen von als Sondermüll 201 deponierenden Resten ( Aschenanteile , Metalle usw ) nach der Umsetzung nach konventionellen an.The processing is very costly and involves various processes, but not all materials can be recycled. This is why large quantities of residues (ash, metals, etc.) are generated after conventional processing and are disposed of as hazardous waste.

Eine Lösung für dieses Problem wird durch die nachstehend beschriebene Erfindung geboten.A solution to this problem is provided by the invention described below.

Die Erfindung , kurz als WTE -Anlage bezeichnet, besteht aus folgenden wesentlichen Komponenten.The invention, briefly referred to as WTE plant, consists of the following essential components.

(siehe Fig. 1) :(see Fig. 1):

1. Automatische Sortierung1. Automatic sorting

- Fe- Abscheider
- Ne-Abscheider- Fe separator
- Ne separator

- Glas/Keramik-Abscheider- Glass/ceramic separator

2. Feinsiebentwässerungspartie2. Fine screen dewatering section

3. Fermenter3. Fermenter

4. Dampferzeuger4. Steam generator

5. Vergaser5. Carburettor

6. Energieerzeugungseinheit6. Power generation unit

7. Untergeordnete Systeme wie Fördereinrichtungen bzw Medienvorsorgung, Steuerungstechnik, Lagertechnik. usw7. Subordinate systems such as conveyor systems or media supply, control technology, storage technology, etc.

8. Optionalen Systemen wie Shift- Reaktor, gegebenenfalls Gasreinigung, Sterilisationsmodul usw.8. Optional systems such as shift reactor, gas purification if necessary, sterilization module, etc.

Funktionsbeschreibung der WTE-AnlageFunctional description of the WTE plant

Die Abfalle werden aus einen Vorlagebehälter mit einen Förderer einer halb- oder vollautomatische Sortiereinheit zugeführt. Diese muß mindestens einen Fe Abscheider (Eisenabscheider) , Ne- Abscheider (Nichteisenmetallabscheider) sowie einen Abscheider für Glas und Keramik umfassen.The waste is fed from a storage container with a conveyor to a semi- or fully automatic sorting unit. This must include at least one Fe separator (iron separator), Ne separator (non-ferrous metal separator) and a separator for glass and ceramics.

Die auf diese Weise abgeschiedenen Stoffe können Wahlweise recycled oder aber deponiert werden.The materials separated in this way can either be recycled or disposed of in landfills.

Der nicht abgeschiedene Müll (also Kunststoffe, Papier; Karton; Verpackungen, Speisereste, biogene bzw organische Abfalle) wird in der Folge über eine Feinsiebentwässerungpartie geleitet.The waste that is not separated (i.e. plastics, paper, cardboard, packaging, food scraps, biogenic or organic waste) is then passed through a fine screen dewatering section.

Diese Feinsiebentwässerungspartie hat eine enge Maschenweise vorzugsweise unter 15mm und dient der Entwässerung des Mülls. Das dabei anfallende verschmutzte Wasser wird in der Folge einem Fermenter zur Vergärung und Biogasgewinnung zugeführt.This fine screen dewatering section has a narrow mesh, preferably under 15mm, and is used to dewater the waste. The resulting contaminated water is then fed into a fermenter for fermentation and biogas production.

Die verbliebenen Feststoffe (Grobfraktion ) werden einer optional en Pelletierung zugeführt .The remaining solids (coarse fraction) are optionally pelletized.

Die dabei produzierten Pellets ( oder das geshredderte Inputmaterial) werden in einem Vergaser unter Zugabe von Wasserdampf und/oder Luft vergast . Für die Funktion des Verfahrens ist es gleichgültig nach welchem Prinzip der Vergaser arbeitet bzw. ob ein-oder mehrstufig vergast wird.The pellets produced (or the shredded input material) are gasified in a gasifier with the addition of steam and/or air. The function of the process does not depend on the principle on which the gasifier works or whether gasification takes place in one or more stages.

Wesentlich ist ,dass Konstanter oder batchmäßiger Ascheaustrag gegeben ist.It is essential that ash discharge is constant or in batches.

Um den Energieinhalt des bei der Vergasung entstehenden Synthesegases zu erhöhen, wird das bei der Fermentation des verschmutzten Abwassers erstehende Biogas vorzugsweise in den Vergaser geleitet.In order to increase the energy content of the synthesis gas produced during gasification, the biogas produced during the fermentation of the contaminated wastewater is preferably fed into the gasifier.

Der zum Betrieb des Vergasers verwendete Dampf kann ganz oder teilweise durch Verdampfen des den Fermenter verlassenden (aufgearbeiteten ) Abwassers bereitgestellt werden.The steam used to operate the gasifier can be provided entirely or partially by evaporation of the (treated) wastewater leaving the fermenter.

Das im Vergaser enstehende Synthesegas kann optional einer Wasserdampf-Shiftreaktion unterzogen werden ,wobei Kohlenmonoxid mittels Wasserdampf und Unter Abspaltung von Wasserstoff zu Kohlendioxid oxidiert wird. Optional kann auch eine Reinigung des Synthesegases folgen.The synthesis gas produced in the gasifier can optionally be subjected to a water vapor shift reaction, whereby carbon monoxide is oxidized to carbon dioxide using water vapor and with the elimination of hydrogen. The synthesis gas can also optionally be purified.

Das Synthesegas kann nunmehr einer energetischen Verwertung in z.B. Kraftwärmekopplungen, Brennstoffzellen, Gasturbinen oder Motoren zugeführt werden.The synthesis gas can now be used for energy recovery in, for example, combined heat and power plants, fuel cells, gas turbines or engines.

Claims (7)

1. Anlage zur Behandlung und Entsorgung von Abfällen, dadurch gekennzeichnet, dass die Anlage mindestens einen Vergaser zur Umsetzung der Abfälle in Synthesegas, sowie mindestens ein Modul zur energetischen Verwertung des Synthesegases umfasst. 1. Plant for the treatment and disposal of waste, characterized in that the plant comprises at least one gasifier for converting the waste into synthesis gas, as well as at least one module for the energetic utilization of the synthesis gas. 2. Anlage nach Anspruch 1 bis 2, dadurch gekennzeichnet, dass eine Feinsiebentwässerungspartie in die Anlage integriert ist. 2. Plant according to claim 1 to 2, characterized in that a fine screen dewatering section is integrated into the plant. 3. Anlage nach Anspruch 1 bis 3, dadurch gekennzeichnet, dass zur Vergärung des Abwassers aus der Feinsiebentwässerungspartie mindestens ein Fermenter in die Anlage integriert ist. 3. Plant according to claim 1 to 3, characterized in that at least one fermenter is integrated into the plant for fermenting the waste water from the fine screen dewatering section. 4. Anlage nach Anspruch 1-4, dadurch gekennzeichnet, dass eine Rohrleitung von mindestens einem Fermenter zu mindestens einem Vergaser derart ausgebildet ist, dass das im Fermenter enstehende Biogas diesem Vergaser regelbar zugeführt werden kann. 4. Plant according to claims 1-4, characterized in that a pipeline from at least one fermenter to at least one gasifier is designed such that the biogas produced in the fermenter can be controllably fed to this gasifier. 5. Anlage nach Anspruch 1-5, dadurch gekennzeichnet, dass eine Rohrleitung zwischen Fermenter und Verdampfer ausgeführt ist, in welche ein Dampferzeugungsmodul integriert ist. 5. Plant according to claims 1-5, characterized in that a pipeline is arranged between the fermenter and the evaporator, into which a steam generation module is integrated. 6. Anlage nach Anspruch 1 bis 6 dadurch gekennzeichnet, dass die Anlage vorzugsweise vor der Vergasung eine Pelletiereinheit beinhaltet. 6. Plant according to claims 1 to 6, characterized in that the plant preferably includes a pelletizing unit before gasification. 7. Anlage nach Anspruch 1 bis 7, dadurch gekennzeichnet, dass das Energieerzeugungsmodul als Blockheizkraftwerk und/oder Brennstoffzelle ausgebildet ist. 7. Plant according to claims 1 to 7, characterized in that the energy generation module is designed as a combined heat and power plant and/or fuel cell.
DE20014110U 1999-12-23 2000-08-16 Plant for the treatment and disposal of waste Expired - Lifetime DE20014110U1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
AT217499 1999-12-23

Publications (1)

Publication Number Publication Date
DE20014110U1 true DE20014110U1 (en) 2001-02-22

Family

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003006387A3 (en) * 2001-07-12 2003-03-20 Adam Krylowicz The method and system of generating methane and electrical energy and thermal
WO2007037768A1 (en) * 2005-09-28 2007-04-05 Gep Yesil Enerji Uretim Teknolojileri Limited Sirketi Solid waste gasification
FR2927983A1 (en) * 2008-02-21 2009-08-28 Dms Treating filth or waste, comprises subjecting filth or waste to compression to separate into a putrescible fraction and a dry fraction, and subjecting the putrescible fraction to an anaerobic digestion to produce biogas
WO2011010002A1 (en) * 2009-07-20 2011-01-27 D.M.S. Method for totally gasifying of garbage or waste
US8559870B2 (en) 2008-08-28 2013-10-15 Centre National D'etudes Spatiales Method and system for acquiring and repatriating satellite data
DE102014202190A1 (en) * 2014-02-06 2015-08-06 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Method and device for generating electrical energy by gasification of solids, in particular biomass

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003006387A3 (en) * 2001-07-12 2003-03-20 Adam Krylowicz The method and system of generating methane and electrical energy and thermal
WO2007037768A1 (en) * 2005-09-28 2007-04-05 Gep Yesil Enerji Uretim Teknolojileri Limited Sirketi Solid waste gasification
FR2927983A1 (en) * 2008-02-21 2009-08-28 Dms Treating filth or waste, comprises subjecting filth or waste to compression to separate into a putrescible fraction and a dry fraction, and subjecting the putrescible fraction to an anaerobic digestion to produce biogas
US8559870B2 (en) 2008-08-28 2013-10-15 Centre National D'etudes Spatiales Method and system for acquiring and repatriating satellite data
WO2011010002A1 (en) * 2009-07-20 2011-01-27 D.M.S. Method for totally gasifying of garbage or waste
DE102014202190A1 (en) * 2014-02-06 2015-08-06 Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. Method and device for generating electrical energy by gasification of solids, in particular biomass

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Legal Events

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R207 Utility model specification

Effective date: 20010329

R150 Utility model maintained after payment of first maintenance fee after three years

Effective date: 20040317

R151 Utility model maintained after payment of second maintenance fee after six years

Effective date: 20070130

R152 Utility model maintained after payment of third maintenance fee after eight years

Effective date: 20090112

R071 Expiry of right