EP0259510A1 - Hélice transporteuse pour fours métallurgiques en particulier fours à sole tournante - Google Patents

Hélice transporteuse pour fours métallurgiques en particulier fours à sole tournante Download PDF

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Publication number
EP0259510A1
EP0259510A1 EP86112533A EP86112533A EP0259510A1 EP 0259510 A1 EP0259510 A1 EP 0259510A1 EP 86112533 A EP86112533 A EP 86112533A EP 86112533 A EP86112533 A EP 86112533A EP 0259510 A1 EP0259510 A1 EP 0259510A1
Authority
EP
European Patent Office
Prior art keywords
coolant
screw conveyor
central shaft
hollow shaft
chambers
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
EP86112533A
Other languages
German (de)
English (en)
Other versions
EP0259510B1 (fr
Inventor
John K. Pargeter
John A. Macdougall
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.)
Vodafone GmbH
Original Assignee
Mannesmann 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 Mannesmann AG filed Critical Mannesmann AG
Priority to AT86112533T priority Critical patent/ATE60432T1/de
Priority to DE8686112533T priority patent/DE3677223D1/de
Publication of EP0259510A1 publication Critical patent/EP0259510A1/fr
Application granted granted Critical
Publication of EP0259510B1 publication Critical patent/EP0259510B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B9/00Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
    • F27B9/14Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment
    • F27B9/16Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity characterised by the path of the charge during treatment; characterised by the means by which the charge is moved during treatment the charge moving in a circular or arcuate path
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B13/00Making spongy iron or liquid steel, by direct processes
    • C21B13/10Making spongy iron or liquid steel, by direct processes in hearth-type furnaces
    • C21B13/105Rotary hearth-type furnaces
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B9/00Furnaces through which the charge is moved mechanically, e.g. of tunnel type; Similar furnaces in which the charge moves by gravity
    • F27B9/30Details, accessories, or equipment peculiar to furnaces of these types
    • F27B9/38Arrangements of devices for charging
    • 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
    • F27D3/00Charging; Discharging; Manipulation of charge
    • F27D3/08Screw feeders; Screw dischargers

Definitions

  • the invention relates to a screw conveyor for metallurgical furnaces, in particular for hearth furnaces, consisting of a rotationally drivable central shaft and a coil or conveying elements connected to it, coolant being able to be conducted through a bore in the central shaft and the central shaft being connected to a rotatable coolant supply and a rotatable coolant discharge is.
  • the direct reduction of iron oxide and other metal oxides can be done in a hearth furnace, particularly in a rotary hearth furnace, using pelletized or briquetted feed that is placed on the stove.
  • Such a rotary hearth furnace is a continuous reheating furnace which is generally provided with a cylindrical inner wall which is arranged at a certain distance from a cylindrical outer wall. The space in between contains the actual rotary hearth. In order to retain the heat generated inside the oven, the walls are relatively low so that the lid can be close to the stove. Burners can be arranged in the inner and outer walls as well as in the lid.
  • the material to be reduced is usually fed or dropped onto the rotary hearth with a conveyor belt or chute. After the material has been transported on the stove, it is removed with a screw conveyor. Because of the associated high temperatures (704 to 1260 degrees C), the screw conveyor is filled with water chilled. Such a screw conveyor is known from US Pat. No. 3,433,931. The gases are drawn off through a smoke duct arranged in the cover.
  • a conventional screw conveyor consists of a central shaft with a solid spiral welded onto it. A coolant is passed through a hole in the central shaft.
  • a plurality of helixes spaced apart from one another are used around the shaft.
  • the screw conveyor Because of the corroding effect of the gases and materials in the rotary hearth furnace and the high temperatures in the furnace, the screw conveyor often fails. The coils wear out overall. Corrosion and erosion, caused by high temperatures and interfering elements (sodium, sulfides, lead crystal, zinc, tin, iron, nickel and chromium) inside the furnace, erode the screw conveyor and make it unusable after only three months. Expensive materials such as high-alloy steels (20% nickel, 20% chromium, rest iron) did not lead to a better result.
  • plumy fine material collects in the spaces between the spirals, which tends to cake. This fine material acts like a sponge, which absorbs and concentrates the corrosive gases present in the furnace.
  • the present invention is based on the object of proposing an improved screw conveyor which can better withstand the harsh operating conditions of an oven.
  • the central shaft is formed at its ends from a tube section, that between the ends there is a hollow shaft which surrounds the tube sections by means of caps, that chambers are subsequently formed on the caps, the coolant channels being one the pipe sections are connected via openings to one of the chambers and that helices or conveying elements through which coolant flows are connected to the hollow shaft, the coolant channels of which are connected to the chamber via slots.
  • This not only cools the central shaft and the hollow shaft, but also the helix or conveyor elements, which results in a considerable improvement in durability.
  • a tube is arranged concentrically to the hollow shaft in the interior thereof between the chambers, which tube is open towards one of the chambers and which has openings in the region of the opposite end for the flow of coolant from a chamber, the hollow shaft are.
  • the coolant thus flows through the screw in two stages: once through the coils and then in countercurrent through the hollow shaft before it is diverted to the outlet.
  • the screw conveyor according to the invention can also be produced very economically by at least the hollow shaft being made from mild steel.
  • the coils or the conveying elements are provided with a support made of corrosion and erosion resistant material. Such material wears extremely little with appropriate internal cooling.
  • the corrosion and erosion resistant material consists of hard metal.
  • FIG. 1 shows a greatly simplified illustration of a rotary hearth furnace 10.
  • the rotary hearth furnace 10 consists of an insulated outer wall 12 and an insulated inner wall 14.
  • a rotary hearth 16 rotates within the rotary hearth furnace 10 in the direction indicated by the arrow 18.
  • a plurality of burners 20 are arranged distributed in the rotary hearth furnace 10.
  • Curtains 22 divide the rotary hearth furnace 10 into clearly separated sections. Material is placed on the stove with a loading device mounted in the lid (which is not shown) of the rotary hearth furnace 10.
  • the material is removed by the screw conveyor 26 and conveyed into a bunker (not shown) for later processing.
  • the screw conveyor 26 is driven by a motor and a mechanical linkage 28. Water is supplied to the screw conveyor 26 as a coolant through the coupling 30.
  • the screw conveyor 26 includes a hollow shaft 32 which is attached to two pipe sections 62, each of which has a bore 34 for the coolant flow (water).
  • a plurality of hollow auger coils 36 surround the hollow shaft 32. The use of six or seven coils 36 is preferred because more coils would tend to cause particles to stick between the coils 36.
  • the coils 36 are shown as right-handed helical lines.
  • the screw conveyor 26 rotates in the direction 38.
  • the coolant water is conducted into the screw conveyor at the water coupling end and exits at the drive end 42.
  • the coils 36 are hollow so that the coolant (water) can flow through them. Slots 46 in two sections of the hollow shaft 32 (see FIG. 4) allow the coolant to flow from the bore 34 into the coil 36 and vice versa.
  • a corrosion-resistant pad 44 can be attached to the front edge of the helix 36.
  • hard metal has been used as support 44, which however, in some cases cracked after a period of time. The cracks then spread into the coil 36 and caused small coolant leaks. Although experience with certain carbide grades has sometimes caused problems, these are preferred for use as pad 44.
  • Figure 4 shows a detail of the screw conveyor 26.
  • the ends 40 and 42 are attached to suitable fasteners (not shown) to ensure watertightness of the entire system and to allow the screw conveyor 26 to rotate.
  • the coolant flow is indicated by arrows 48.
  • the caps 74 and 76 prevent coolant from escaping from the screw conveyor 26.
  • the hollow shaft 32 with a series of internal baffles, causes the coolant to flow in a serpentine or countercurrent flow before exiting the screw.
  • the water flow (arrow 48) first flows from the (water coupling) end 40 through the pipe section 62 and then enters a chamber 50.
  • the chamber 50 has openings 52 that cause the coolant to flow into a second chamber 54 and then through the slots 46 into the coils 36.
  • only one slot 46 is shown at the (water coupling) end (or near end) 40, it goes without saying that the number of slots 46 is exactly the same as the number of coils 36.
  • the entire length of the coolant flows through the coils 36 to the distal end 42, where it re-enters the hollow shaft 32 through the slot 46 and a chamber 72.
  • the coolant then continues to flow through the opening 68 formed in a partition 66 an annular space 56 between the hollow shaft 32 and an inner tube 58. Spacers 64 maintain the distance between the hollow shaft 32 and the inner tube 58.
  • the coolant flows in the opposite direction to the partition wall 60, where it is redirected again and forced to flow in the inner tube 58.
  • the coolant now flowing through the inner tube 58 flows through the opening in the partition 66 towards the distal end 42 and then out of the screw conveyor 26.
  • the screw conveyor lasted about two to three times longer than a conventional water-cooled screw conveyor. Such screw conveyors lasted only two to three months, while the screw conveyor according to the invention had a service life of four to nine months.
  • the pitch, pitch angle, length and number of coils 36 are of course dependent on the size of the stove, the environment and the material to be processed in the stove. Under special conditions, the temperature in the rotary hearth furnace was approximately 982 degrees C and the coils were approximately 4.9 m long. Hollow shaft 32 was approximately 0.45 m in diameter and the entire hollow shaft was 5.2 m long. The pitch angle 68 was about 35 degrees 15 ⁇ , and the pitch 70 about 33.8 cm (see FIG. 2). Because of the cooling for the screw conveyor 26, the coolant entered the screw conveyor 26 at a temperature of approximately 32.2 degrees Celsius and exited at approximately 49 degrees Celsius with a flow rate of approximately 1136 l / min. and about 69 to 103 kpa.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Furnace Charging Or Discharging (AREA)
  • Screw Conveyors (AREA)
  • Tunnel Furnaces (AREA)
EP86112533A 1985-04-03 1986-09-10 Hélice transporteuse pour fours métallurgiques en particulier fours à sole tournante Expired - Lifetime EP0259510B1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
AT86112533T ATE60432T1 (de) 1986-09-10 1986-09-10 Foerderschnecke fuer metallurgische oefen, insbesondere fuer herdoefen.
DE8686112533T DE3677223D1 (de) 1986-09-10 1986-09-10 Foerderschnecke fuer metallurgische oefen, insbesondere fuer herdoefen.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US06/719,310 US4636127A (en) 1985-04-03 1985-04-03 Conveying screw for furnace

Publications (2)

Publication Number Publication Date
EP0259510A1 true EP0259510A1 (fr) 1988-03-16
EP0259510B1 EP0259510B1 (fr) 1991-01-23

Family

ID=24889569

Family Applications (1)

Application Number Title Priority Date Filing Date
EP86112533A Expired - Lifetime EP0259510B1 (fr) 1985-04-03 1986-09-10 Hélice transporteuse pour fours métallurgiques en particulier fours à sole tournante

Country Status (5)

Country Link
US (1) US4636127A (fr)
EP (1) EP0259510B1 (fr)
BR (1) BR8601447A (fr)
DE (1) DE3610490A1 (fr)
IN (1) IN165587B (fr)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19543074C2 (de) * 1995-11-13 1999-07-15 Mannesmann Ag Direktreduktionsverfahren und Einrichtung zur Durchführung des Verfahrens
CN105300108A (zh) * 2015-10-22 2016-02-03 桐乡市耀润电子有限公司 用于铁氧体球形颗粒原料进入预烧窑的落料设备
CN105300107A (zh) * 2015-10-22 2016-02-03 桐乡市耀润电子有限公司 用于铁氧体球形颗粒原料进入预烧窑的落料装置
CN105333737A (zh) * 2015-10-22 2016-02-17 桐乡市耀润电子有限公司 铁氧体球形颗粒原料进入预烧窑的落料设备
CN107572199A (zh) * 2017-10-26 2018-01-12 江苏清溢环保设备有限公司 一种新型螺旋式进料装置

Families Citing this family (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5885521A (en) * 1994-12-16 1999-03-23 Midrex International B.V. Rotterdam, Zurich Branch Apparatus for rapid reduction of iron oxide in a rotary hearth furnace
US5730775A (en) * 1994-12-16 1998-03-24 Midrex International B.V. Rotterdam, Zurich Branch Method for rapid reduction of iron oxide in a rotary hearth furnace
DE19529925A1 (de) * 1995-08-01 1997-02-06 Mannesmann Ag Verfahren und Vorrichtung zur Eingabe von Schüttgut in einen Drehherdofen
US5972066A (en) * 1997-04-22 1999-10-26 Iron Dynamics, Inc. Mixed bed iron reduction process
US5863197A (en) * 1997-04-25 1999-01-26 The International Metals Reclamation Company, Inc. Solid flight conveying screw for furnace
US6152729A (en) * 1997-08-28 2000-11-28 Maumee Research & Engineering, Inc. Spray cooled furnace discharge assembly
US5924861A (en) * 1997-08-28 1999-07-20 Maumee Research & Engineering, Incorporated Furnace discharge assembly
US6120577A (en) * 1998-03-25 2000-09-19 Ltv Steel Company, Inc. Treatment of steel mill waste metal oxides
JP3404309B2 (ja) * 1999-01-18 2003-05-06 株式会社神戸製鋼所 還元鉄塊成物の製造方法および製造装置
US6390810B1 (en) 1999-03-15 2002-05-21 Maumee Research & Engineering, Inc. Method and apparatus for reducing a feed material in a rotary hearth furnace
CN1306045C (zh) 1999-08-30 2007-03-21 株式会社神户制钢所 粒状还原铁原料的供给方法及其装置
JP4287572B2 (ja) 2000-04-26 2009-07-01 株式会社神戸製鋼所 回転式炉床炉
JP3866492B2 (ja) 2000-06-29 2007-01-10 株式会社神戸製鋼所 回転炉床式還元炉の操業方法
US6814924B2 (en) * 2001-10-22 2004-11-09 Kobe Steel, Ltd. Rotary hearth furnace and screw thereof for discharging reduced iron
JP4866899B2 (ja) * 2006-04-06 2012-02-01 新日鉄エンジニアリング株式会社 回転炉床式還元炉の還元鉄排出用スクリューコンベヤ
US8518146B2 (en) 2009-06-29 2013-08-27 Gb Group Holdings Limited Metal reduction processes, metallurgical processes and products and apparatus
US8726804B1 (en) 2009-07-29 2014-05-20 Larry E. Koenig System and method for adjusting and cooling a densifier
US9403336B2 (en) 2010-12-09 2016-08-02 Mark E. Koenig System and method for crushing and compaction
US8851409B2 (en) 2010-12-09 2014-10-07 Mark E. Koenig System for crushing
US8708266B2 (en) 2010-12-09 2014-04-29 Mark E. Koenig System for crushing with screw porition that increases in diameter
US9586770B2 (en) 2011-08-05 2017-03-07 Mark E. Koenig Material waste sorting system and method
US9346624B2 (en) 2011-11-04 2016-05-24 Mark E. Koenig Cantilevered screw assembly
US9132968B2 (en) * 2011-11-04 2015-09-15 Mark E. Koenig Cantilevered screw assembly
CN104713371B (zh) * 2015-03-13 2016-05-11 南京航空航天大学 烧结环冷机矿料摊平装置及方法
JP6601046B2 (ja) * 2015-08-05 2019-11-06 日本製鉄株式会社 高炉内の原料排出用スクリューコンベア
US9821962B2 (en) 2015-12-14 2017-11-21 Mark E. Koenig Cantilevered screw assembly
US10434483B2 (en) * 2017-02-15 2019-10-08 Wenger Manufacturing Inc. High thermal transfer hollow core extrusion screw assembly
US11358895B2 (en) * 2018-11-15 2022-06-14 Owens-Brockway Glass Container Inc. Batch charger for a melting chamber

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Publication number Priority date Publication date Assignee Title
GB1153782A (en) * 1965-09-10 1969-05-29 Midland Ross Corp Process for making Metallized Pellets from Iron Oxide Containing Material
DE1921884A1 (de) * 1968-04-29 1970-03-19 Joy Mfg Co Umlaufende Bearbeitungsvorrichtung
FR2361621A1 (fr) * 1976-08-12 1978-03-10 Ciba Geigy Ag Serpentin d'echangeur thermique et son procede de fabrication
CH649046A5 (de) * 1979-05-18 1985-04-30 Omg Pessina Perobelli Auflader fuer papierwaren, insbesondere signaturen, bogen oder hefte in einer buchbindereimaschine.

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US233320A (en) * 1880-10-19 Auger or forcing-screw for brick and tile machines
US192069A (en) * 1877-06-19 Improvement in grain conveyers and driers
DE350467C (de) * 1922-03-18 August Pertz Ventillose Schmierpumpe fuer Vor- und Rueckwaertsgang
US2297289A (en) * 1939-07-31 1942-09-29 Collis Company Furnace discharging device
US3020025A (en) * 1957-08-29 1962-02-06 Richard F O'mara Rotary heat exchanger
NO122742B (fr) * 1970-05-16 1971-08-02 Stord Bartz Industri As
US3764062A (en) * 1972-02-28 1973-10-09 Pennwalt Corp Centrifuge apparatus
US3777810A (en) * 1972-08-24 1973-12-11 Strong Mfg Co Scott Dryer
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Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1153782A (en) * 1965-09-10 1969-05-29 Midland Ross Corp Process for making Metallized Pellets from Iron Oxide Containing Material
DE1921884A1 (de) * 1968-04-29 1970-03-19 Joy Mfg Co Umlaufende Bearbeitungsvorrichtung
FR2361621A1 (fr) * 1976-08-12 1978-03-10 Ciba Geigy Ag Serpentin d'echangeur thermique et son procede de fabrication
CH649046A5 (de) * 1979-05-18 1985-04-30 Omg Pessina Perobelli Auflader fuer papierwaren, insbesondere signaturen, bogen oder hefte in einer buchbindereimaschine.

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19543074C2 (de) * 1995-11-13 1999-07-15 Mannesmann Ag Direktreduktionsverfahren und Einrichtung zur Durchführung des Verfahrens
CN105300108A (zh) * 2015-10-22 2016-02-03 桐乡市耀润电子有限公司 用于铁氧体球形颗粒原料进入预烧窑的落料设备
CN105300107A (zh) * 2015-10-22 2016-02-03 桐乡市耀润电子有限公司 用于铁氧体球形颗粒原料进入预烧窑的落料装置
CN105333737A (zh) * 2015-10-22 2016-02-17 桐乡市耀润电子有限公司 铁氧体球形颗粒原料进入预烧窑的落料设备
CN105300108B (zh) * 2015-10-22 2017-07-21 桐乡市耀润电子有限公司 用于铁氧体球形颗粒原料进入预烧窑的落料设备
CN105300107B (zh) * 2015-10-22 2017-07-21 桐乡市耀润电子有限公司 用于铁氧体球形颗粒原料进入预烧窑的落料装置
CN107572199A (zh) * 2017-10-26 2018-01-12 江苏清溢环保设备有限公司 一种新型螺旋式进料装置

Also Published As

Publication number Publication date
BR8601447A (pt) 1986-12-09
DE3610490C2 (fr) 1988-03-31
EP0259510B1 (fr) 1991-01-23
DE3610490A1 (de) 1986-10-16
IN165587B (fr) 1989-11-25
US4636127A (en) 1987-01-13

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