WO1993000450A1 - Heat processing apparatus - Google Patents

Heat processing apparatus Download PDF

Info

Publication number
WO1993000450A1
WO1993000450A1 PCT/GB1992/001120 GB9201120W WO9300450A1 WO 1993000450 A1 WO1993000450 A1 WO 1993000450A1 GB 9201120 W GB9201120 W GB 9201120W WO 9300450 A1 WO9300450 A1 WO 9300450A1
Authority
WO
WIPO (PCT)
Prior art keywords
chamber
circulation means
kiln
gases
input end
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
PCT/GB1992/001120
Other languages
English (en)
French (fr)
Inventor
Ophneil Henry Perry
Geoffrey Riley
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.)
Stein Atkinson Stordy Ltd
Original Assignee
Stein Atkinson Stordy Ltd
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 Stein Atkinson Stordy Ltd filed Critical Stein Atkinson Stordy Ltd
Priority to CA 2112249 priority Critical patent/CA2112249C/en
Priority to US08/167,998 priority patent/US5451033A/en
Priority to AU20214/92A priority patent/AU666315B2/en
Publication of WO1993000450A1 publication Critical patent/WO1993000450A1/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D13/00Apparatus for preheating charges; Arrangements for preheating charges
    • F27D13/002Preheating scrap
    • 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
    • B03B9/00General arrangement of separating plant, e.g. flow sheets
    • B03B9/06General arrangement of separating plant, e.g. flow sheets specially adapted for refuse
    • B03B9/061General arrangement of separating plant, e.g. flow sheets specially adapted for refuse the refuse being industrial
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • C22B1/005Preliminary treatment of scrap
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B21/00Obtaining aluminium
    • C22B21/0007Preliminary treatment of ores or scrap or any other metal source
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2201/00Pretreatment
    • F23G2201/50Devolatilising; from soil, objects
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2900/00Special features of, or arrangements for incinerators
    • F23G2900/52002Rotary drum furnaces with counter-current flows of waste and gas
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling
    • 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S266/00Metallurgical apparatus
    • Y10S266/901Scrap metal preheating or melting

Definitions

  • This invention relates to apparatus for heat processing scrap materials in the recovery of their useful constituents and removal as by vapourization or burning of contaminants such as lacquer or paint coatings.
  • the invention is particularly but not exclusively applicable to scrap metal materials, for example in the recycling of metal containers typically aluminium or aluminium alloy beverage cans.
  • the object of the present invention is to provide heat processing apparatus for the above purpose, e.g. incorporating a rotary kiln, which is economical to manufacture and install, compact, adaptable in design, and affective and efficient in operation.
  • apparatus for heat processing scrap material to separate contaminants therefrom comprising a kiln defining an enclosed furnace chamber having a feed path extending therethrough along which a flow of the mater.- al is passed in use between material input and ma-erial output ends of the chamber: and gas circulation means for providing a flow of heated gases through the chamber to act on said flow of material in use: characterised in that said circulation means includes an inlet duct extending into the kiln from the material input end and opening into the chamber adjacent the output end, and an outlet flue opening from the chamber at said input end whereby the flow of gases within the chamber acting directly on the material is in the opposite direction of travel to the passage of the material along said path, and those parts of the gas circulation means which are outside the kiln are all located at or adjacent to the material input end thereof
  • the kiln is a rotary kiln centered on an inclined axis and the inlet duct is disposed co axially therein. Said duct may rotate in common with the kiln.
  • Said gas circulation means may include a recirculation connection externally of the kiln and at or adjacent said input end thereof for operative recirculation of at least part of the gases exhausted from the furnace through the outlet flue.
  • Said circulation means may further include flow inducing means for forced movement of gases through the furnace: control means for regulating the operating temperature of the gases an after burner for high temperature disposal or breaking down of the contaminant content of the gases so exhausted at a higher temperature than the operating temperature within the chamber; and/or cooling means acting on the gases fed to the inlet duct to reduce their temperature to a predetermined level.
  • the apparatus comprises a rotary kiln 10 defining an enclosed furnace chamber 12.
  • the axis of the kiln is inclined so that it slopes downwardly from its material input end 14 to its material output end 16 i.e. from left to right as viewed in the drawing.
  • the extremities of the rotating kiln being provided with airtight seals 13.20 connecting it with respective non-rotating upper and lower enclosure formations 22.24 at said respective endc in conventional manner .
  • the scrap material is fed into the chamber from a hopper or the like (not shown) through a delivery chute 26 opening into inlet end 14 to pass along a feed path through the rotating kiln, exiting from a discharge chute 28 at the output end 16 to drop onto a conveyor 30.
  • Gas circulation means of the apparatus comprises an inlet duct 32 extending co-axially of chamber 12 through the rotating kiln 10 to open into said chamber within closure formation 24 i.e. at the material output end of the chamber.
  • Duct 32 is conveniently mounted for rotation with kiln 10, its upper end opening through the end wall of the closure formation 22 at the material input end of the chamber by way of a further airtight seal 34.
  • Heated gases at controlled temperature are fed into duct 32 from an ante-chamber 36 defined by fixed structure of the gas circulation means all of which is at or immediately adjacent to said material input end 14.
  • the gas flow within chamber 12 is operated at negative pressure, i.e. less than ambient atmospheric pressure in the manner described in our said co-pending application GB-A-2229801 to avoid any escape of contaminated gases e.g. if there should be any leakage past the various seals.
  • Said negative pressure is induced by a centrifugal fan 38 in an outlet flue 40 opening from the top of closure formation 22 at the material input end 14 of chamber 12
  • Flue 40 opens into the upper end of a vertical after burner chamber 42 disposed alongside ante-chamber 36 and containing a gas fuelled or other burner head 44, the temperature in chamber 42 being such that the lacquer and other contaminant content of the exhaust gases is further broken down at a higher temperature than that in the kiln chamber 12.
  • the gases exiting from the bottom of chamber 42 pass into the ante-chamber 36, a proportion thereof being recirculated through the kiln chamber 12 as described above and a proportion being led off from ante ⁇ chamber 36 through a branch duct 46 for after-treatment and eventual disposal. Provision (not shown) may be made for cooling the gases fed into furnace chamber 12.
  • Delivery chute 26 is preferably arranged so that the material passing therethrough is preheated, e.g. in part by radiant heat from the upper end of inlet duct 32. for drying the material and raising its temperature before it enters the chamber 12, again providing increased efficiency of operation and minimising heat loss.
  • Control means are provided for monitoring and regulating the operating temperatures in chamber 12 and elsewhere, regulating the flow rate of the gases etc as described in our said application G3-A-2229801.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • Manufacturing & Machinery (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Metallurgy (AREA)
  • General Engineering & Computer Science (AREA)
  • Muffle Furnaces And Rotary Kilns (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
  • General Preparation And Processing Of Foods (AREA)
  • Furnace Details (AREA)
  • Heating, Cooling, Or Curing Plastics Or The Like In General (AREA)
PCT/GB1992/001120 1991-06-28 1992-06-19 Heat processing apparatus Ceased WO1993000450A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
CA 2112249 CA2112249C (en) 1991-06-28 1992-06-19 Heat processing apparatus
US08/167,998 US5451033A (en) 1991-06-28 1992-06-19 Heat processing apparatus
AU20214/92A AU666315B2 (en) 1991-06-28 1992-06-19 Heat processing apparatus

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB9114030.1 1991-06-28
GB9114030A GB2257239B (en) 1991-06-28 1991-06-28 Heat processing apparatus

Publications (1)

Publication Number Publication Date
WO1993000450A1 true WO1993000450A1 (en) 1993-01-07

Family

ID=10697519

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/GB1992/001120 Ceased WO1993000450A1 (en) 1991-06-28 1992-06-19 Heat processing apparatus

Country Status (12)

Country Link
US (1) US5451033A (https=)
EP (1) EP0523858B1 (https=)
AT (1) ATE145434T1 (https=)
AU (1) AU666315B2 (https=)
CA (1) CA2112249C (https=)
DE (1) DE69215284T2 (https=)
DK (1) DK0523858T3 (https=)
ES (1) ES2094296T3 (https=)
GB (1) GB2257239B (https=)
GR (1) GR3022514T3 (https=)
TW (1) TW221462B (https=)
WO (1) WO1993000450A1 (https=)

Families Citing this family (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4304294C2 (de) * 1993-02-12 1995-04-06 Strepp Gmbh & Co Kg Papierfabr Verfahren zur Gewinnung verwertbarer Stoffe aus Verbundmaterial
IT1262420B (it) * 1993-11-03 1996-06-19 In Tec Italia Int Env Tech Srl Dispositivo e procedimento per il pretrattamento di rottame elettronico.
FR2719796B1 (fr) * 1994-05-11 1996-07-05 Ecaa Procédé de production d'aciers en poudre à partir de boues d'usinage mécanique, et dispositif pour la mise en Óoeuvre dudit procédé.
ES2144235T3 (es) * 1995-04-25 2000-06-01 Jarkko Linnainmaa Dispositivo para el tratamiento de residuos metalicos.
ATE205887T1 (de) 1995-12-15 2001-10-15 Rheinfelden Aluminium Gmbh Verfahren und anlage zur rückgewinnung von aluminium aus abfällen und reststoffen
ES2196561T3 (es) * 1997-05-30 2003-12-16 Babcock & Wilcox Volund Aps Procedimiento y aparato de calentamiento de un horno rotativo concebido para la gasificacion y la pirolisis de una materia organica.
RU2162584C2 (ru) * 1999-03-05 2001-01-27 Федоренко Валентин Валентинович Воздухоподогреватель для утилизации тепла дымовых газов
ATE377741T1 (de) * 2001-07-24 2007-11-15 Elti Srl Verfahren zur vorbereitung von im elektroofen zuzuführenden eisenschrott und vorrichtung zur durchführung des verfahrens
GB0506033D0 (en) 2005-03-24 2005-04-27 Perry Ophneil H Apparatus and method for thermally removing coatings and/or impurities
JP2004290727A (ja) * 2003-02-05 2004-10-21 Nissei Kogyo Kk 使用済み缶処理システムおよび使用済み缶処理方法
DE102005021656A1 (de) * 2005-05-06 2006-11-09 Bayer Industry Services Gmbh & Co. Ohg Verfahren zur Rückgewinnung von Metallen aus Abfällen und anderen Materialien mit organischen Bestandteilen
GB2471709B (en) 2009-07-10 2011-06-08 Fanli Meng Furnace
EP2464940B1 (en) 2009-08-14 2018-05-23 Pyrotek, Inc. Waste heat system and method for preheating scrap
GB2575648B (en) 2018-07-17 2020-07-29 North American Construction Service Ltd System for cleaning metallic scraps from organic compounds
CN112080307B (zh) * 2020-10-08 2021-06-22 威海劲变信息科技有限公司 废旧轮胎热解反应炉专用回转耙辊

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB151518A (en) * 1919-12-31 1920-09-30 William J Kuntz Improvements in or relating to rotary driers
US3627289A (en) * 1970-06-22 1971-12-14 Walter Erman Apparatus and method for removing oil from metal turnings
EP0002825A1 (en) * 1977-12-30 1979-07-11 Phillips Petroleum Company Method and apparatus for drying particulate material
GB2229801A (en) * 1989-03-28 1990-10-03 Stein Atkinson Strody Ltd Scrap processing apparatus

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB143707A (en) * 1919-05-16 1920-06-03 Andrew Armstrong Short Improvements in and relating to drying machinery
US1441351A (en) * 1921-06-24 1923-01-09 Henry H Hindshaw Rotating kiln
GB544462A (en) * 1941-01-24 1942-04-14 Ernest Newell & Company Ltd Improvements in or relating to apparatus for drying granulated, pulverulent and other loose material
US4200262A (en) * 1978-07-10 1980-04-29 College Research Corporation Method and apparatus for removing combustible material from metal scrap
JPS6117885A (ja) * 1984-07-03 1986-01-25 株式会社 大和三光製作所 通気式回転乾燥装置
GB2186065A (en) * 1986-01-31 1987-08-05 Henley Burrowes & Company Limi A boiler
GB2229701B (en) * 1986-09-05 1991-04-24 Fibre Glass Evercoat Co Dispensing container
IT1245346B (it) * 1990-04-09 1994-09-20 Blufin Spa Metodo di preriscaldo rottame di ferro tramite pirolisi di residui resinosi in esso contenuti con recupero integrale del loro contenuto energetico e miglioramento del ciclo siderurgico
GB2246191A (en) * 1990-07-06 1992-01-22 Eric Keith Riley Reclaiming metal from scrap

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB151518A (en) * 1919-12-31 1920-09-30 William J Kuntz Improvements in or relating to rotary driers
US3627289A (en) * 1970-06-22 1971-12-14 Walter Erman Apparatus and method for removing oil from metal turnings
EP0002825A1 (en) * 1977-12-30 1979-07-11 Phillips Petroleum Company Method and apparatus for drying particulate material
GB2229801A (en) * 1989-03-28 1990-10-03 Stein Atkinson Strody Ltd Scrap processing apparatus

Also Published As

Publication number Publication date
GR3022514T3 (en) 1997-05-31
DE69215284T2 (de) 1997-03-20
ATE145434T1 (de) 1996-12-15
AU666315B2 (en) 1996-02-08
TW221462B (https=) 1994-03-01
DE69215284D1 (de) 1997-01-02
EP0523858A1 (en) 1993-01-20
CA2112249A1 (en) 1993-01-07
US5451033A (en) 1995-09-19
EP0523858B1 (en) 1996-11-20
DK0523858T3 (da) 1997-01-13
CA2112249C (en) 2004-05-11
AU2021492A (en) 1993-01-25
GB2257239B (en) 1995-09-13
ES2094296T3 (es) 1997-01-16
GB2257239A (en) 1993-01-06
GB9114030D0 (en) 1991-08-14

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