EP2928986B1 - Vorrichtung in form eines thermolyse-rotations-reaktors und verfahren zum betreiben eines solchen in einer anordnung zur thermischen zersetzung von abprodukten und abfällen - Google Patents

Vorrichtung in form eines thermolyse-rotations-reaktors und verfahren zum betreiben eines solchen in einer anordnung zur thermischen zersetzung von abprodukten und abfällen Download PDF

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Publication number
EP2928986B1
EP2928986B1 EP13826992.3A EP13826992A EP2928986B1 EP 2928986 B1 EP2928986 B1 EP 2928986B1 EP 13826992 A EP13826992 A EP 13826992A EP 2928986 B1 EP2928986 B1 EP 2928986B1
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EP
European Patent Office
Prior art keywords
tools
rotating
thermolysis
shaft
outer jacket
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
EP13826992.3A
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German (de)
English (en)
French (fr)
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EP2928986A1 (de
Inventor
Hartwig Streitenberger
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.)
Hs Techtransfer Ug (haftungsbeschraenkt) & Cokg
Original Assignee
Hs Techtransfer Ug (haftungsbeschrankt) & CoKg
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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B7/00—Coke ovens with mechanical conveying means for the raw material inside the oven
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B1/00—Retorts
    • C10B1/10—Rotary retorts
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B7/00—Coke ovens with mechanical conveying means for the raw material inside the oven
    • C10B7/10—Coke ovens with mechanical conveying means for the raw material inside the oven with conveyor-screws
    • 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
    • C10J3/007—Screw type gasifiers

Definitions

  • the invention relates to a device in the form of a thermolysis-rotary reactor according to the preamble of the claims and a method for operating such a reactor in an arrangement for the thermal decomposition of waste products and waste.
  • a moving bed gasifier which comprises a carburetor chamber with a carburetor space and a carburetor, wherein the carburetor space is surrounded by a carburetor shell and having a synthesis gas outlet at its one, closed end and communicating via its second, open end via the carburetor shell with the carburetor ,
  • the carburetor is in its interior formed as a carburetor pot into which an entry device and at least one feed lead.
  • the gasifier pot on a recessed bottom with respect to the gasifier chamber, the bottom opens into a central shaft.
  • Stirrer which are rotatably mounted in the carburetor pot via a stirrer shaft, wherein the agitator shaft is surrounded by a conveyor.
  • the carburetor pot encloses with the carburetor jacket an insulation space through which the entry device, the feed, central shaft and the agitator shaft are guided with conveying device, wherein the carburetor base casing supports this.
  • a carburetor dome is arranged in the manner that a gap is generated between the carburetor dome and the carburetor jacket and / or the carburetor.
  • thermolysis reactor comprising an outer sheath and an inner sheath forming a double sheath, the inner sheath being surrounded by the outer sheath such that between the inner sheath and the outer sheath a gap exists, the double jacket has an entry, a discharge, at least one gasification agent Einitati and a distributor and the inner shell encloses an interior, which is bounded at the ends of lids.
  • the gap at the ends of the double jacket formed by the inner jacket and outer sheath closes against the environment and the covers support a shaft, wherein in the gap and the shaft is a heat carrier, the shaft is mounted centrally in the lids and carries a delivery tool.
  • thermolysis reactor is according to DE 10 2009 007 768.5 used to carry out a process in which the thermolysis reactor is tilted so that the discharge is above the entry.
  • the shaft is driven and in the shaft and the double jacket heated liquid heat carrier is generated and moved.
  • This liquid heat carrier is fluidically guided in the gap by the guide, wherein the material to be treated is guided by means of conveying tool from the entry in the direction of discharge and heated in this transport by means of supplied gasification agent.
  • thermochemical reaction stop A continuous and stable temperature-controlled control of the process is no longer possible. The process comes to a standstill. Due to this unstable process control, not only is the demolition of the entire pyrolysis process occurring, but also local overheating and thus distortion of the thermolysis chamber. Regardless of the extremely fluctuating gas quality, the thermochemical reduction of the material is not completed and thus leads to adverse process conditions of subsequent arrangements. From the DE 199 32 822 A1 and the DE 196 14 689 A1 Feeders for reactors in the form of a conveyor or screw conveyor are known. These conveyors also have the disadvantages listed above.
  • DE 27 25 650 A1 discloses an apparatus and method for heating volatiles-containing solid materials.
  • WO 2010/096038 A1 discloses a screw gasifier.
  • the object of the present invention is to provide a device in the form of a thermolysis-rotary reactor, which avoids the above-mentioned disadvantages of the prior art, in particular a forced movement of the material to be treated in the reactor organized, not the existing bed of thermolysis reaction destroys and prevents blockages in the reactor as well as slag and separate embers, in order to ensure stable and uniform process control of the thermolysis process.
  • this object is achieved by the characterizing features of the first and the ninth patent claim. Further favorable embodiments of the invention are specified in the subordinate claims.
  • thermolysis-rotary reactor of a tubular outer shell with end-capping lids, an interior, one in the lids centrally stored wave, entry tools and discharge tools, which are placed at the beginning or at the end of the shaft within the thermolysis-rotary reactor, wherein on the shaft spiral runner helixes are fixed and the runner helical spirals, one or more times, near the Inside the outer shell are arranged in the interior and have a square, rectangular, round or oval shape, characterized in that at the beginning and at the end of the shaft insertion tools and discharge tools are placed, which are movable by means of the shaft by a drive unit, wherein the entry tools within the effective range of the spiral runner helixes are arranged simply or multiply parallel to the shaft and below a Guteintrages.
  • thermolysis-rotary reactor is in a horizontal storage on a frame.
  • thermolysis-rotary reactor is operated in such a way that the Gutaustrag positioned at the opposite end below the Guteintrages and the shaft is driven externally via a drive unit, wherein the material to be treated mixed and loosened by means of entry tools, then by means of skids- Coils is transported axially and radially, and the material flow through the Vergasungsffeneinträge and the VergasungsffenJraum with a gasification agent, preferably with hot air and mixed oxygen for initiating exothermic and endothermic processes, is applied.
  • a gasification agent preferably with hot air and mixed oxygen for initiating exothermic and endothermic processes
  • the gasification agent flows under slight negative pressure and without interruption and destruction of the ember bed only by the material flow.
  • FIG. 1 shows a thermolysis-rotary reactor, which consists of a tubular outer shell (1), in whose interior (3) takes place a thermo-chemical reaction in the form of an autothermal degassing (partial oxidation) of the raw material under a slight negative pressure.
  • This outer shell (1) has at its two ends in each case a the interior (3) final lid (2) and is surrounded by an insulation (16).
  • insertion tools (6) and discharge tools (7) are placed inside the thermolysis-rotary reactor and are movable by a drive unit (10).
  • a Guteintrag (8) is arranged and below the discharge tools (7) located in the wall of the reactor, a Gutaustrag (9).
  • thermolysis-rotary reactor two divided and perforated VergasugsffenJöchte (11) are arranged axially and centrally in the lower part of the wall of the thermolysis-rotary reactor.
  • separate gasification agent entries (12) and a gas outlet (13) are passed through the wall of the thermolysis-rotation reactor.
  • the gas discharge (13) is arranged laterally above in the entry area.
  • lock A (14) and lock B (15) are arranged.
  • pressure reliefs (16) and various measuring nozzles (17) are still passed.
  • the thermolysis-rotary reactor is surrounded by a thermal insulation (18) and is mounted horizontally on a frame (19).
  • the runner coils (5) are spirally, one or more times, executed near the inside of the tubular outer shell (1) in the interior (3) of the thermolysis-rotary reactor.
  • the runner coils (5) have a square, rectangular, round or oval shape.
  • the entry tools (6) may have a square, rectangular, round or oval shape,
  • the discharge tools (7) above the Gutaustrags (9) are arranged simply or repeatedly.
  • the discharge tools (7) may have a square, rectangular, round or oval shape.
  • the gasification agent shafts (11) are preferably perforated or slotted.
  • the Guteitrag (8) preferably has a rotary valve.
  • thermolysis-rotary reactor The gas outlet (13) of the thermolysis-rotary reactor can be placed both centrally and at the end and the lock A (14) and the lock B (15) are preferably designed as a rotary valve.
  • the thermolysis-rotary reactor is preferably arranged horizontally on a frame (19) (horizontal storage).
  • This thermolysis-rotary reactor is operated as follows: The solid (selected, shredded, preheated and predried) waste materials, hereinafter referred to as good, are fed via the product feed (8) into the interior (3) of the thermolysis-rotary reactor. The entry of the goods is such that only very small amounts of ambient air with enter the interior (3).
  • a rotary valve is preferably used.
  • the inner space (3) surrounded by the tubular outer casing (1) and the laterally closing lids (2) carries the centrally arranged shaft (4) with insertion tools (6), runner spirals (5) and discharge tools (7), wherein in the operating state by the rotational movement of the shaft (4) with said attachments a continuous transport of the goods from Guteintrag (8) to the Gutaustrag (9).
  • the shaft (4) is guided centrally in the lids (2) on the entry and discharge side and driven by an external drive unit (10).
  • the material passes preferably at a temperature of 50 ° C to 100 ° C, an edge length of about 35 mm and a residual moisture content of 10 to 15 Ma% in the thermolysis-rotation reactor.
  • gasification agent preferably enriched oxygen air
  • the gasification agent entries (12) and their distribution via the gasification agent shafts (11) installed in the lower region the gasification agent passes into the interior (3) of the thermolysis-rotation reactor.
  • the resulting reaction gas flows through the flow of material, the reaction mixture, up into the free space (3) and is proportionately taken through the gas outlet (13) and passed into the next unit. Separately, the resulting thermolysis coke is discharged over the Gutaustrag (10) or forwarded to the next unit.
  • the material By the supply of heat via the gasification agent, the material is residue-dried and then pyrolyzed.
  • the gases released in this thermal process react proportionally with the gasification agent and thus generate part of the required process heat.
  • the gasification agent is metered to the extent that a targeted smoldering of the goods takes place. This is preferably done at temperatures of 350 to 550 ° C.
  • the complete product has become carbonaceous solid particles and implemented hydrocarbon process gas. All solid and proportionate gaseous components are discharged via the Gutaustrag (9).
  • the supply of separated carbon preferably from the following units, is provided via a lock A (14).
  • Another lock B (15) allows the supply of additives, preferably lime.
  • the pressure relief (16) installed in the upper tubular outer casing (1) serves to relieve pressure.
  • thermolysis-rotary reactor To ensure the procedural process control located in the tubular outer shell (1), preferably in an axial arrangement, measuring nozzle (17) for receiving sensors.
  • the entire thermolysis-rotary reactor is thermally insulated to stabilize the process temperature via an insulation (18) and mounted on a frame (19), which allows a longitudinal expansion due to thermal expansion.
  • the main advantages of the thermolysis-rotary reactor according to the invention are that it organizes a uniform and forced movement of the material to be treated in the reactor, the existing bed of thermolysis reaction is not destroyed and thus blockages in the reactor and slag and separate Glutnester prevented to ensure stable and uniform process control of the thermolysis process.
  • the continuous undulating course of the flow of goods prevents interruptions, the destruction of the ember bed, nesting and hotspots.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Processing Of Solid Wastes (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
EP13826992.3A 2012-12-04 2013-12-01 Vorrichtung in form eines thermolyse-rotations-reaktors und verfahren zum betreiben eines solchen in einer anordnung zur thermischen zersetzung von abprodukten und abfällen Active EP2928986B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102012024204.2A DE102012024204B4 (de) 2012-12-04 2012-12-04 Vorrichtung in Form eines Thermolyse-Rotations-Reaktors und Verfahren zum Betreiben eines solchen in einer Anordnung zur thermischen Zersetzung von Abprodukten und Abfällen
PCT/DE2013/000783 WO2014086334A1 (de) 2012-12-04 2013-12-01 Vorrichtung in form eines thermolyse-rotations-reaktors und verfahren zum betreiben eines solchen in einer anordnung zur thermischen zersetzung von abprodukten und abfällen

Publications (2)

Publication Number Publication Date
EP2928986A1 EP2928986A1 (de) 2015-10-14
EP2928986B1 true EP2928986B1 (de) 2019-02-13

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EP13826992.3A Active EP2928986B1 (de) 2012-12-04 2013-12-01 Vorrichtung in form eines thermolyse-rotations-reaktors und verfahren zum betreiben eines solchen in einer anordnung zur thermischen zersetzung von abprodukten und abfällen

Country Status (9)

Country Link
US (1) US9969936B2 (ja)
EP (1) EP2928986B1 (ja)
JP (1) JP6192735B2 (ja)
CN (1) CN105026521B (ja)
CA (1) CA2893790C (ja)
DE (1) DE102012024204B4 (ja)
HK (1) HK1214289A1 (ja)
RU (1) RU2648720C2 (ja)
WO (1) WO2014086334A1 (ja)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102016121046B4 (de) 2016-11-04 2018-08-02 HS TechTransfer UG (haftungsbeschränkt) & Co. KG Duplex-TEK-Mehrstufen-Vergaser
DE202016106184U1 (de) 2016-11-04 2016-11-17 Hartwig Streitenberger Duplex-TEK-Mehrstufen-Vergaser
BR202018070746U8 (pt) * 2018-10-08 2022-08-16 Arildo Falcade Junior Me Gaseificador de resíduos sólidos e líquidos
CN114410321A (zh) * 2022-01-04 2022-04-29 江苏鹏飞集团股份有限公司 用于含锌废油漆处理的热解回转窑

Family Cites Families (30)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SU386974A1 (ru) * 1972-01-31 1973-06-21 У. К. Зиемелис, Н. А. Бракш, К. М. Абеле , Л. К. Дубава Институт ХИМКИ древесины Латвийской ССР Реактор для скоростного термолиза
GB1553196A (en) 1975-08-20 1979-09-26 London Brick Buildings Ltd Mixer for and method of mixing particulate constituents
GB1585584A (en) 1976-06-08 1981-03-04 Kobe Steel Ltd Process and apparatus for heating solid materials containing volatile matter
IT1083562B (it) 1977-07-04 1985-05-21 Olivetti & Co Spa Mobile metallico ad elementi componibili
US4123332A (en) * 1977-09-06 1978-10-31 Energy Recovery Research Group, Inc. Process and apparatus for carbonizing a comminuted solid carbonizable material
DE3126049A1 (de) * 1981-07-02 1983-01-13 Hölter, Heinz, Dipl.-Ing., 4390 Gladbeck "pyrolysereaktor mit statischem reaktorkoerper und rotierender, vorzugsweise schneckenartiger materialfoerder- und -umwaelzeinrichtung"
FR2546178B1 (fr) * 1983-05-20 1990-09-21 Gagneraud Pere Fils Entreprise Procede de desulfuration des gaz a l'aide de bains mineraux fondus lors de la gazeification de produits carbones
US4591362A (en) 1984-04-06 1986-05-27 Phillips Petroleum Company Fluid injection method
JP2736152B2 (ja) * 1990-03-26 1998-04-02 三井造船株式会社 ごみ焼却灰の再処理装置
JP3291656B2 (ja) * 1991-01-09 2002-06-10 三井造船株式会社 ごみ焼却灰の再処理装置
JPH06312172A (ja) * 1993-04-28 1994-11-08 Mitsui Eng & Shipbuild Co Ltd 焼却灰の処理方法および装置
JP3597251B2 (ja) * 1995-04-06 2004-12-02 川崎重工業株式会社 湿潤固体の熱処理装置
JPH09279161A (ja) * 1996-04-10 1997-10-28 Nippon Steel Corp 廃プラスチック熱分解炉
DE19614689C2 (de) * 1996-04-13 1999-11-04 Maximilian Bauknecht Multivalent einsetzbare Anlage zur thermischen Behandlung von Ausgangssubstanzen
SK279397B6 (sk) * 1997-03-03 1998-11-04 Ivan Ma�Ar Spôsob termálnej a/alebo katalytickej dekompozície
DE19843613C2 (de) 1998-09-23 2000-12-07 Harald Martin Verfahren und Vorrichtung zur Aufarbeitung von Abprodukten und Abfallstoffen
DE19932822C2 (de) * 1999-07-14 2003-11-20 Johann Hochreiter Vorrichtung zum Entgasen von organischen Substanzen
DE19934070C1 (de) * 1999-07-23 2001-04-05 Ruhstrat Gmbh Rohrofen mit einem Brennrohr und einer in dem Brennrohr angeordneten Förderschnecke
JP4434752B2 (ja) * 2002-04-10 2010-03-17 株式会社荏原製作所 廃棄物のガス化溶融システム
WO2007065202A1 (en) * 2005-12-05 2007-06-14 Struan Glen Robertson Apparatus for treating materials
JP2009536260A (ja) * 2006-05-05 2009-10-08 プラスコエナジー アイピー ホールディングス、エス．エル．、ビルバオ シャフハウゼン ブランチ 炭素質原料のガスへの変換のための制御システム
US9051522B2 (en) * 2006-12-01 2015-06-09 Shell Oil Company Gasification reactor
US7993131B2 (en) * 2007-08-28 2011-08-09 Conocophillips Company Burner nozzle
US8377155B2 (en) 2008-02-20 2013-02-19 Robert C. Tyer Auger gasifier with continuous feed
HUP0800262A2 (en) 2008-04-24 2009-10-28 Lekrinszki Balazs Barna Transport apparatus for reactor and reactor
DE202008017561U1 (de) * 2008-11-20 2009-10-29 Eurotherm Technologies Ag Vorrichtung in Form eines Bewegt-Bett-Vergasers
DE102009007768B4 (de) * 2009-02-05 2015-07-16 Hartwig Streitenberger Vorrichtung in Form eines Thermolysereaktors und Verfahren zum Betreiben eines solchen in einer Anordnung zur thermischen Zersetzung von Abprodukten und Abfällen
JP2012525488A (ja) * 2009-04-30 2012-10-22 プライム グループ アライアンス， エルエルシー バイオマスおよび他の炭素系物質の構成物質取得のためのシステムおよび方法
US8394240B2 (en) * 2009-07-14 2013-03-12 C2O Technologies, Llc Process for treating bituminous coal by removing volatile components
WO2012168945A1 (en) * 2011-06-10 2012-12-13 Bharat Petroleum Corporation Limited Process for co-gasification of two or more carbonaceous feedstocks and apparatus thereof

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
None *

Also Published As

Publication number Publication date
US9969936B2 (en) 2018-05-15
RU2015126860A (ru) 2017-01-12
DE102012024204B4 (de) 2018-02-01
JP2016508863A (ja) 2016-03-24
CA2893790A1 (en) 2014-06-12
US20150322347A1 (en) 2015-11-12
CN105026521A (zh) 2015-11-04
DE102012024204A1 (de) 2014-06-05
WO2014086334A1 (de) 2014-06-12
EP2928986A1 (de) 2015-10-14
HK1214289A1 (zh) 2016-07-22
CA2893790C (en) 2022-01-04
JP6192735B2 (ja) 2017-09-06
CN105026521B (zh) 2018-01-09
RU2648720C2 (ru) 2018-03-28

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