WO1990010683A1 - Procede pour decharger du coke refroidi a sec provenant d'une tour d'extinction de coke, et dispositif correspondant - Google Patents

Procede pour decharger du coke refroidi a sec provenant d'une tour d'extinction de coke, et dispositif correspondant Download PDF

Info

Publication number
WO1990010683A1
WO1990010683A1 PCT/EP1990/000348 EP9000348W WO9010683A1 WO 1990010683 A1 WO1990010683 A1 WO 1990010683A1 EP 9000348 W EP9000348 W EP 9000348W WO 9010683 A1 WO9010683 A1 WO 9010683A1
Authority
WO
WIPO (PCT)
Prior art keywords
coke
lock
drum
gas
discharge
Prior art date
Application number
PCT/EP1990/000348
Other languages
German (de)
English (en)
Inventor
Gerd Nashan
Wilhelm Stewen
Horst Dungs
Willi Brinkmann
Robert Hoffmann
Willi Kissmann
Manfred Rudel
Original Assignee
Still Otto 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 Still Otto Gmbh filed Critical Still Otto Gmbh
Publication of WO1990010683A1 publication Critical patent/WO1990010683A1/fr
Priority to KR1019910701119A priority Critical patent/KR920701395A/ko

Links

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
    • C10B33/00Discharging devices; Coke guides
    • C10B33/12Discharge valves
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G65/00Loading or unloading
    • B65G65/30Methods or devices for filling or emptying bunkers, hoppers, tanks, or like containers, of interest apart from their use in particular chemical or physical processes or their application in particular machines, e.g. not covered by a single other subclass
    • B65G65/34Emptying devices
    • B65G65/40Devices for emptying otherwise than from the top
    • B65G65/48Devices for emptying otherwise than from the top using other rotating means, e.g. rotating pressure sluices in pneumatic systems
    • B65G65/4881Devices for emptying otherwise than from the top using other rotating means, e.g. rotating pressure sluices in pneumatic systems rotating about a substantially horizontal axis
    • 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
    • C10B39/00Cooling or quenching coke
    • C10B39/02Dry cooling outside the oven

Definitions

  • the invention relates to a method for discharging dry-cooled coke from a coke cooling shaft, the coke being withdrawn from the coke cooling shaft and then from the coke disc continuously or in batches via non-gas-tight extraction devices, preferably by actuating discharge rockers arranged uniformly over the cooling shaft cross section gastight system is removed and a device for performing this method.
  • the invention is therefore based on the object of proposing a method and a device for discharging dry-cooled coke of the type defined at the outset, which are improved with regard to the problems described.
  • a gas-tight, wear-resistant discharge system with a low overall height and low investment costs should also be obtained.
  • Claim 9 contains a device for performing the method. Preferred embodiments are given in claims 10 and 11.
  • the cooled coke is then extracted from a preferably square or rectangular coke cooling shaft z. B. by actuating discharge rockers discontinuously and discharged via a cellular lock which ensures the gas-tight closure, preferably via a drum lock equipped with two lock chambers.
  • each of the two lock chambers of the drum lock can be at least the one thrown off a discharge rocker
  • the amount of coke thrown from a discharge rocker can be accommodated in one of the two lock chambers of a two-chamber drum lock, the drum lock not being moved during the coke discharge over the discharge rockers arranged above the drum lock and this being emptied first, so ⁇ as soon as the last coke has reached the receiving lock chamber from the discharge rocker actuated.
  • the drum lock When the drum lock is actuated, it is pivoted through 180 °, so that the entire coke, which had previously reached the lock chamber which is ready to receive via the discharge rocker, falls out downwards and z. B. is discharged in a metered manner via a subsequently arranged vibration channel.
  • the movement and thus the emptying of the two-chamber drum lock is locked with the actuation of the discharge rockers in such a way that the lock chamber is only emptied after the coke flow has come to a complete standstill via the respective discharge rocker.
  • coke-side overshoot and thus overfilling of the two lock chambers with wear of the housing wall and any sealing strips due to clamped coke pieces is prevented at all times.
  • the invention alternatively provides that the discontinuously withdrawn coke is fed with the aid of a vibrating trough to a continuously operating cellular wheel sluice with a large number of sluice chambers.
  • the vibrating trough can be arranged above the cell wheel lock for the transition to the continuous further transport of the coke and, on the other hand, below the drum lock.
  • a residual cushion of coke can form on the vibrating channel in the discharge funnel, which can also contain the quantity of several coke batches thrown off with the discharge rockers.
  • This residual coke is expediently monitored by level probes and regulated by changing the discharge quantity in the vibratory trough and the rotary valve. In any case, it should be ensured that between the discharge rockers and the upper edge of the residual coke pad in the discharge funnel there is a free space for the even addition of the cooling gas below the discharge rockers.
  • the invention provides that the sheet metal dividing the sluice in two chambers is connected on the outside to circular segments or other side plates adapted to the circular part of the housing shell, which are also rotated by 180 ° when the sluice chambers are emptied.
  • These circular segments form a largely gastight seal with respect to the housing jacket. They are at least as large as the inlet and outlet openings of the drum lock. This ensures that the cooling gas, which is under pressure above the lock, cannot flow directly to the outside during the emptying or rotation of the lock chambers.
  • FIGS. 1 and 2 show the two-chamber drum lock (4) according to the invention with the vibration channel (5) arranged underneath and in FIGS. 3 and 4 the arrangement of the vibration channel (17) above a rotary valve (18).
  • the coke is usually cooled in the cooling shaft by a circulating cooling gas.
  • the cooled coke is withdrawn in a metered manner at the end of the square or rectangular cooling shaft via the curved coke chutes (2) and by alternately actuating the discharge rockers (3), a large number of discharge rockers being evenly distributed over the shaft cross section.
  • the entire coke bed rests on a sort of sieve tray, with the cooling gas below the discharge rockers (3) being distributed evenly over the cross-section of the cooling shaft.
  • the actuation of the discharge rockers (3) is controlled via the final coke temperature.
  • the coke falls directly and completely from the discharge rockers (3) via the outlet funnel (9) into the upper chamber (13) of the drum lock (4) which holds the coke.
  • the inner movable part of the drum sluice with the sheet metal (12) and the circular segments (15) attached to it are rotated by 180 ° around the central horizontal axis of rotation, the coke being released from the chamber which now releases coke ( 14) onto the vibration channel (5) underneath and from there evenly to a conveyor belt (6) for further transport.
  • the two-chamber drum lock shown in FIGS. 1 and 2 is characterized in that the essentially circular drum space of the drum lock (4) is divided into two lock chambers by a flat plate (12) which can be rotated about a central horizontal axis. So that the coke does not come into contact with the inner wall of the circular part of the casing (16) and grinds along it when the drum lock is actuated, circular segments (16) which are adapted to the circular part of the casing (16) are attached to the ends of the sheet (12). 15) or similar side panels attached.
  • cooling gas can be prevented from escaping through the introduction of inert gas (N ⁇ application (11)) at the inlet port of the drum lock.
  • the vibrating trough is arranged directly under the discharge funnel (9) in order to ensure an even application to the To ensure cellular wheel sluice (18).
  • two vibrating troughs (17) and the associated cell wheels (18) and the conveyor belts (6) can also be arranged next to one another.
  • the discharge funnel (9) is constructed in such a way that all of the coke thrown off the coke discharge rockers (3) can be removed either from one or the other vibrating channel.
  • a needle slide (21) can be arranged in the outlet funnel (9).
  • E REPLACEMENT LEAF (8) for the coke cooling shaft (1) is supported on the supporting walls (7).
  • the drum sluice (4) with the further transport organs for the coke is expediently supported separately, a compensator (10) being attached to compensate for expansion between the discharge funnel and the drum sluice (4).

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Coke Industry (AREA)

Abstract

On retire le coke de la tour d'extinction de coke (1) de manière discontinue, en charges, à travers des dispositifs d'évacuation non étanches aux gaz, de préférence en actionnant des bascules de décharge (3) agencées à des intervalles réguliers sur la section transversale de la tour d'extinction (1), puis on fait sortir ce coke du système étanche aux gaz par des écluses. On décharge le coke qui est extrait de manière discontinue de la tour d'extinction de coke (1) à travers une écluse à roue cellulaire (18) qui assure l'étanchéité par rapport aux gaz, de préférence une écluse en tambour (4) dotée de deux chambres d'écluse (13, 14). L'invention porte également sur un dispositif pour la mise en oeuvre de ce procédé.
PCT/EP1990/000348 1989-03-16 1990-03-02 Procede pour decharger du coke refroidi a sec provenant d'une tour d'extinction de coke, et dispositif correspondant WO1990010683A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1019910701119A KR920701395A (ko) 1989-03-16 1991-09-16 코크스 냉각 샤프트에서 건조한 냉각 코크스를 반출하는 방법 및 장치

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DEP3908534.1 1989-03-16
DE3908534A DE3908534C1 (fr) 1989-03-16 1989-03-16

Publications (1)

Publication Number Publication Date
WO1990010683A1 true WO1990010683A1 (fr) 1990-09-20

Family

ID=6376439

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/EP1990/000348 WO1990010683A1 (fr) 1989-03-16 1990-03-02 Procede pour decharger du coke refroidi a sec provenant d'une tour d'extinction de coke, et dispositif correspondant

Country Status (4)

Country Link
EP (1) EP0462992A1 (fr)
KR (1) KR920701395A (fr)
DE (1) DE3908534C1 (fr)
WO (1) WO1990010683A1 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018210204A1 (fr) * 2017-05-16 2018-11-22 山东汉菱电气有限公司 Dispositif de traitement de matériau, groupe et système associés, et procédé destiné à être utilisé dans le traitement de matériaux organiques
CN113403092A (zh) * 2021-07-16 2021-09-17 中煤能源研究院有限责任公司 一种密封旋转式低水分熄焦排焦装置

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19625462A1 (de) * 1996-06-26 1998-01-15 Motan Fuller Verfahrenstechnik Verfahren und Vorrichtung zum Befüllen einer Dichtstrom-Förderleitung
CN110980177B (zh) * 2019-11-28 2021-11-05 苏州嘉诺环境工程有限公司 一种炉前给料系统

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE960759C (de) * 1954-07-02 1957-03-28 Otto & Co Gmbh Dr C Austragkasten fuer einen senkrechten Ofen
AU5742773A (en) * 1973-06-27 1975-01-09 William White Robert Improvements in and relating to goal carbonisation
DE3429292A1 (de) * 1984-08-09 1986-02-20 Carl Still Gmbh & Co Kg, 4350 Recklinghausen Verfahren zur entstaubung von trocken gekuehltem koks
WO1986001819A1 (fr) * 1984-09-17 1986-03-27 Nippon Steel Corporation Procede et appareil de decharge d'une substance pulverulente et granulee d'un fourneau vertical hermetique de refroidissement

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6042398B2 (ja) * 1983-04-30 1985-09-21 新日本製鐵株式会社 竪型炉の粉粒体排出装置
JPS6474289A (en) * 1987-09-14 1989-03-20 Nippon Steel Corp Quenching technique in discharge device of coke dry quenching equipment

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE960759C (de) * 1954-07-02 1957-03-28 Otto & Co Gmbh Dr C Austragkasten fuer einen senkrechten Ofen
AU5742773A (en) * 1973-06-27 1975-01-09 William White Robert Improvements in and relating to goal carbonisation
DE3429292A1 (de) * 1984-08-09 1986-02-20 Carl Still Gmbh & Co Kg, 4350 Recklinghausen Verfahren zur entstaubung von trocken gekuehltem koks
WO1986001819A1 (fr) * 1984-09-17 1986-03-27 Nippon Steel Corporation Procede et appareil de decharge d'une substance pulverulente et granulee d'un fourneau vertical hermetique de refroidissement

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018210204A1 (fr) * 2017-05-16 2018-11-22 山东汉菱电气有限公司 Dispositif de traitement de matériau, groupe et système associés, et procédé destiné à être utilisé dans le traitement de matériaux organiques
CN113403092A (zh) * 2021-07-16 2021-09-17 中煤能源研究院有限责任公司 一种密封旋转式低水分熄焦排焦装置

Also Published As

Publication number Publication date
EP0462992A1 (fr) 1992-01-02
KR920701395A (ko) 1992-08-11
DE3908534C1 (fr) 1990-05-31

Similar Documents

Publication Publication Date Title
DE2442836A1 (de) Katalysatorueberfuehrungsverfahren fuer bewegtbett-reaktoren
WO1990010683A1 (fr) Procede pour decharger du coke refroidi a sec provenant d'une tour d'extinction de coke, et dispositif correspondant
DE2857119C1 (de) Vertikaler zylindrischer Kompostierbehaelter
DE4212097C2 (fr)
DE8106130U1 (de) Einrichtung und verfahren zum abtrennen von in einem gasstrom mitgefuehrten feinteiligen feststoffen
DE1767577A1 (de) Verfahren und Vorrichtung zur Malzgewinnung
DE2253353A1 (de) Sortiereinrichtung
DE2516442C3 (de) Beschickungsvorrichtung für einen Hochofen
DE3706654A1 (de) Schachtofen-beschickungsanlage
DE1229822B (de) Vorrichtung zum Zerkleinern von Sintergut
EP0036576B1 (fr) Réacteur à lit de boulets avec un dispositif pour matériel absorbant et procédé pour son fonctionnement
EP0756572B1 (fr) Dispositif de prelevement dose de solides en vrac
DE2115159A1 (de) Gerat zum Extrahieren von in pflanz hchem Material enthaltenen Substanzen durch Diffusion
DE10232279B4 (de) Verfahren zum Befüllen eines Horizontalkammerkoksofens
DE3328209A1 (de) Vorrichtung zum gleichmaessigen beschicken von zylindrischen schaechten
DE19628413C2 (de) Modular erweiterbares Komponentensystem zur biologischen Behandlung von organisch-biologischen Abfällen
EP0615113B1 (fr) Dispositif pour le dosage de matériaux en vrac
DE2621477A1 (de) Automatische waage
DE626516C (de) Schleudermaschine
DE242372C (fr)
DE3504848C1 (de) Entstaubungsvorrichtung für Mischer, insbesondere Betonmischer
DE2229088C2 (de) Kugelmühle zum Aufbereiten von gebrauchtem Gießereiformsand
DE632729C (de) Vorrichtung zum Schwelen von Brennstoffen in einzelnen Behaeltern
DE3727233A1 (de) Schuettgutzufuhr- und gasabfuhr-einrichtung, insbesondere fuer gegenstrom-wanderbettfilter
DE882284C (de) Vorrichtung zum Reifen von Alkalicellulose

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): KR US

AL Designated countries for regional patents

Kind code of ref document: A1

Designated state(s): AT BE CH DE DK ES FR GB IT LU NL SE

WWE Wipo information: entry into national phase

Ref document number: 1990903824

Country of ref document: EP

WWP Wipo information: published in national office

Ref document number: 1990903824

Country of ref document: EP

WWR Wipo information: refused in national office

Ref document number: 1990903824

Country of ref document: EP

WWW Wipo information: withdrawn in national office

Ref document number: 1990903824

Country of ref document: EP