EP0685551A1 - Intern beheizter Drehofen zur Pyrolyse von Abfällen - Google Patents

Intern beheizter Drehofen zur Pyrolyse von Abfällen Download PDF

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Publication number
EP0685551A1
EP0685551A1 EP95401177A EP95401177A EP0685551A1 EP 0685551 A1 EP0685551 A1 EP 0685551A1 EP 95401177 A EP95401177 A EP 95401177A EP 95401177 A EP95401177 A EP 95401177A EP 0685551 A1 EP0685551 A1 EP 0685551A1
Authority
EP
European Patent Office
Prior art keywords
heating means
oven
solid materials
oven according
waste
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
EP95401177A
Other languages
English (en)
French (fr)
Other versions
EP0685551B1 (de
Inventor
Gérard Martin
Eric Marty
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.)
IFP Energies Nouvelles IFPEN
Original Assignee
IFP Energies Nouvelles IFPEN
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Filing date
Publication date
Application filed by IFP Energies Nouvelles IFPEN filed Critical IFP Energies Nouvelles IFPEN
Publication of EP0685551A1 publication Critical patent/EP0685551A1/de
Application granted granted Critical
Publication of EP0685551B1 publication Critical patent/EP0685551B1/de
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B1/00Retorts
    • C10B1/10Rotary retorts
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B11/00Machines or apparatus for drying solid materials or objects with movement which is non-progressive
    • F26B11/02Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles
    • F26B11/026Arrangements for charging or discharging the materials to be dried, e.g. discharging by reversing drum rotation, using spiral-type inserts
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B11/00Machines or apparatus for drying solid materials or objects with movement which is non-progressive
    • F26B11/02Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles
    • F26B11/04Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles rotating about a horizontal or slightly-inclined axis
    • F26B11/0404Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles rotating about a horizontal or slightly-inclined axis with internal subdivision of the drum, e.g. for subdividing or recycling the material to be dried
    • F26B11/0413Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles rotating about a horizontal or slightly-inclined axis with internal subdivision of the drum, e.g. for subdividing or recycling the material to be dried the subdivision consisting of concentric walls, e.g. multi-pass or recirculation systems; the subdivision consisting of spiral-shaped walls
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B11/00Machines or apparatus for drying solid materials or objects with movement which is non-progressive
    • F26B11/02Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles
    • F26B11/04Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles rotating about a horizontal or slightly-inclined axis
    • F26B11/0445Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles rotating about a horizontal or slightly-inclined axis having conductive heating arrangements, e.g. heated drum wall
    • F26B11/045Machines or apparatus for drying solid materials or objects with movement which is non-progressive in moving drums or other mainly-closed receptacles rotating about a horizontal or slightly-inclined axis having conductive heating arrangements, e.g. heated drum wall using heated internal elements, e.g. which move through or convey the materials to be dried
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F5/00Elements specially adapted for movement

Definitions

  • the present invention relates to the field of heat treatment furnaces for solid materials, and more particularly pyrolysis (or thermolysis) furnaces intended to treat solids such as waste of any kind.
  • this type of installation remains complex in particular in terms of the shape of the cylinders; moreover the heating and smoke evacuation means not being fixed, problems may arise at the connections.
  • This type of installation like most ovens known rotary kilns, must be considered rotary kilns with external indirect heating.
  • the present invention represents an improvement of known rotary pyrolysis ovens
  • the heating means comprises at least one tubular element whose branch or branches are parallel to the longitudinal axis of the furnace, the branch or branches are connected by membranes, the assembly having a generally cylindrical shape.
  • a heat transfer fluid circulates in the co-current and / or counter-current heating means for solid materials.
  • the oven according to the invention can comprise tubular elements which are supplied independently of each other.
  • the heating means can constitute an element of generally cylindrical shape around or inside which are arranged resistive elements.
  • the type of oven illustrated in FIG. 1 comprises a rotating cylinder 1 with a horizontal axis or slightly inclined according to the needs for inventory and flow of solids.
  • This cylinder turning is mounted for example on rollers 2, themselves fixed on a base 3 which supports most of the equipment of the oven.
  • Said rotating cylinder is equipped with an assembly 4 which ensures its rotation at a speed preferably between 0.1 and 20 rpm.
  • the transfer from the hopper to the oven takes place in a line 12, in which the waste is more or less compacted if it is present in an abundant form in the raw state.
  • the waste progresses in the device 9 according to a more or less compact piston flow, while being preheated.
  • the waste falls by gravity into the rotating cylinder, and gradually flows longitudinally towards the outlet 8. The waste therefore goes back and forth in the oven.
  • the heating device 9 can consist of a set of tubular elements 20 connected to one another by membranes 21, ensuring continuity over the whole of the device which has a generally cylindrical shape.
  • the tubular elements are preferably grouped by 2, 4, 6, etc. in the form of pins in which a hot fluid circulates or in which a combustion operation is carried out. These pins are connected to a collector 13 fixed on the fixed part 5 or placed near this fixed part 5.
  • the manifold 13 comprises a zone 13a for the supply of hot fluid or for the supply of air and fuel, and a zone 13b for the discharge of the cooled fluid or the fumes. In any case, there is contact between the fluid or the fumes used for heating the tubes 20 on the one hand, and the gases contained in the cylinder 1 and the fixed part 5 on the other hand.
  • the device 9 consists of simple pins having two types of tubes 20: tubes of type 22 in which the fluid circulates cocurrently with the waste inside the device 9 and the tubes of type 23 interposed between the tubes 22 in which the fluid circulates against the current of the waste.
  • the gaseous fuel can be natural gas or even gases resulting from the pyrolytic treatment of waste, said gases having been previously and preferably treated to remove tar and particles which could lead to unwanted fouling phenomena.
  • the heating device 9 could just as easily consist of a substantially cylindrical tube, equipped with electric heating means such as resistors, wound around or at the inside said tube, helically, with connections carried outside to the level of a power supply unit.
  • the oven according to the invention is preferably intended for the treatment of waste at temperatures between 50 and 900 ° C., with final temperatures of the pyrolysis products leaving the oven preferably between 400 and 600 ° C.
  • the temperatures at the heater 9 are between 100 and 2000 ° C and preferably between 600 and 1000 ° C.
  • the tubes 20, 21, 22 provide a first heating (or preheating) of the waste by the internal face of the device 9, during the progression of the latter inside the device 9 itself. The calorific contribution to the waste continues when these have left the device 9, via the external face of said device 9.
  • the heating of the waste is then carried out by the external face of the device 9 which emits energy by radiation, either directly on the waste , or on the internal wall of cylinder 1 which then returns it to the waste.
  • a part of the internal face or of the external face can be hidden by an insulating mask 14, as indicated in FIG. 1, to control and limit the supply of heat at any point of the system.
  • the oven according to the present invention presupposes, a priori, the use for heating, of hot fluids or of clean fuels such as natural gas or pyrolysis gases rid of their tars and other particles.
  • the hot fluid can be air preheated, for example to a temperature between 500 and 1000 ° C., in a boiler which burns raw pyrolysis gases.
  • the present invention has a number of advantages in particular with respect to a conventional installation comprising a rotating cylinder heated externally by burners or a heat transfer fluid which surrounds the rotating cylinder.

Landscapes

  • Engineering & Computer Science (AREA)
  • General Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Thermal Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Sustainable Development (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)
  • Processing Of Solid Wastes (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Incineration Of Waste (AREA)
EP95401177A 1994-05-30 1995-05-19 Intern beheizter Drehofen zur Pyrolyse von Abfällen Expired - Lifetime EP0685551B1 (de)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR9406660A FR2720487B1 (fr) 1994-05-30 1994-05-30 Four tournant de pyrolyse de déchets avec chauffage interne.
FR9406660 1994-05-30

Publications (2)

Publication Number Publication Date
EP0685551A1 true EP0685551A1 (de) 1995-12-06
EP0685551B1 EP0685551B1 (de) 1999-08-25

Family

ID=9463735

Family Applications (1)

Application Number Title Priority Date Filing Date
EP95401177A Expired - Lifetime EP0685551B1 (de) 1994-05-30 1995-05-19 Intern beheizter Drehofen zur Pyrolyse von Abfällen

Country Status (7)

Country Link
US (1) US5644997A (de)
EP (1) EP0685551B1 (de)
CN (1) CN1118665C (de)
AT (1) ATE183770T1 (de)
DE (1) DE69511626T2 (de)
FR (1) FR2720487B1 (de)
PL (1) PL178782B1 (de)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19617617C2 (de) * 1996-05-02 1998-11-12 Buck Chem Tech Werke Verfahren zur Entsorgung von Explosivstoff-Wirkmassen sowie Vorrichtung hierfür
US6189463B1 (en) * 1998-05-12 2001-02-20 General Technology, Inc. Methods and apparatus for incinerating combustible waste material such as farm animal biomass
DE102008030983B4 (de) 2008-06-27 2012-06-06 Corina Projahn Verfahren und Vorrichtung zur Durchführung einer Pyrolyse und deren Verwendung zum Verschwelen von Altreifen und Biomasse
WO2009094962A1 (de) 2008-01-28 2009-08-06 Corina Projahn Verfahren und vorrichtung zur durchführung einer pyrolyse
DE202008008767U1 (de) 2008-06-27 2008-09-11 Projahn, Corina Vorrichtung zur Durchführung einer Pyrolyse
DE202008007674U1 (de) 2008-06-09 2009-02-12 Fittkau, Wilfried, Dipl.-Ing. Anlage zur Erzeugung von Elektroenergie durch Depolimerisation von Polimeren, insbesondere Altreifen
DE102008039817A1 (de) 2008-08-22 2010-02-25 Corina Projahn Pyrolyseprodukt und seine Verwendung
US8833276B2 (en) * 2009-02-06 2014-09-16 William Hunkyun Bang Burner system for waste plastic fuel
FR2944344B1 (fr) 2009-04-10 2013-12-27 Inst Francais Du Petrole Four tournant pour traitement thermique de materiaux solides
FR2948448B1 (fr) 2009-07-21 2014-01-10 Inst Francais Du Petrole Four tournant pour traitement thermique radiatif de materiaux solides
CN102994103A (zh) * 2011-09-14 2013-03-27 邢献军 一种生物质干燥炭化炉
CN103292468B (zh) * 2012-02-24 2017-11-24 江苏圣奥化学科技有限公司 换热器
DE102012109874A1 (de) 2012-10-16 2014-04-17 Merenas Trust Reg. Vorrichtung und Verfahren zur stofflichen Behandlung von Rohstoffen
US8603558B1 (en) 2013-03-27 2013-12-10 Jarrah Ali Abdullah Ali Jaddan Almutairi Waste food recycling machine
CN114739129B (zh) * 2022-04-08 2023-09-26 郑州沃特节能科技股份有限公司 一种基于余热回收再利用的烘干系统

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1508578A (en) * 1923-10-09 1924-09-16 Kohlenscheidungsgesellschaft M Apparatus for the distillation of coal and other substances
US3481720A (en) * 1966-04-29 1969-12-02 Sun Oil Co Process and apparatus for the distillation of solids
US4066024A (en) * 1975-12-24 1978-01-03 Oconnor Chadwell Rotating fluidized bed combustor
DE2903280A1 (de) 1979-01-29 1980-08-28 Peter Voelskow Entgasungsdrehtrommel
EP0056931A1 (de) * 1981-01-27 1982-08-04 VOEST-ALPINE Aktiengesellschaft Drehrohrofen
EP0072164A2 (de) * 1981-08-12 1983-02-16 British Nuclear Fuels PLC Einrichtungen für einen Drehrohrofen
EP0446930A1 (de) * 1990-03-14 1991-09-18 Wayne Technologies Pyrolitisches Konvertierungssystem
FR2668774A1 (fr) 1990-11-07 1992-05-07 Inst Francais Du Petrole Procede et dispositif de production d'un combustible solide a partir de dechets combustibles.

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3861336A (en) * 1973-11-07 1975-01-21 Shinzaburo Koyanagi Garbage incinerator
US4730564A (en) * 1987-06-08 1988-03-15 Abboud Harry I Multi-stage kiln
US5273355A (en) * 1992-04-23 1993-12-28 Astec Industries Inc. Aggregate dryer and soil incinerator

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1508578A (en) * 1923-10-09 1924-09-16 Kohlenscheidungsgesellschaft M Apparatus for the distillation of coal and other substances
US3481720A (en) * 1966-04-29 1969-12-02 Sun Oil Co Process and apparatus for the distillation of solids
US4066024A (en) * 1975-12-24 1978-01-03 Oconnor Chadwell Rotating fluidized bed combustor
DE2903280A1 (de) 1979-01-29 1980-08-28 Peter Voelskow Entgasungsdrehtrommel
EP0056931A1 (de) * 1981-01-27 1982-08-04 VOEST-ALPINE Aktiengesellschaft Drehrohrofen
EP0072164A2 (de) * 1981-08-12 1983-02-16 British Nuclear Fuels PLC Einrichtungen für einen Drehrohrofen
EP0446930A1 (de) * 1990-03-14 1991-09-18 Wayne Technologies Pyrolitisches Konvertierungssystem
FR2668774A1 (fr) 1990-11-07 1992-05-07 Inst Francais Du Petrole Procede et dispositif de production d'un combustible solide a partir de dechets combustibles.

Also Published As

Publication number Publication date
FR2720487A1 (fr) 1995-12-01
US5644997A (en) 1997-07-08
CN1113310A (zh) 1995-12-13
FR2720487B1 (fr) 1996-07-12
PL308842A1 (en) 1995-12-11
PL178782B1 (pl) 2000-06-30
CN1118665C (zh) 2003-08-20
EP0685551B1 (de) 1999-08-25
DE69511626T2 (de) 1999-12-09
ATE183770T1 (de) 1999-09-15
DE69511626D1 (de) 1999-09-30

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