JPH0289988A - Tunnel furnace for secondary firing of graphite materials - Google Patents

Tunnel furnace for secondary firing of graphite materials

Info

Publication number
JPH0289988A
JPH0289988A JP63239974A JP23997488A JPH0289988A JP H0289988 A JPH0289988 A JP H0289988A JP 63239974 A JP63239974 A JP 63239974A JP 23997488 A JP23997488 A JP 23997488A JP H0289988 A JPH0289988 A JP H0289988A
Authority
JP
Japan
Prior art keywords
pitch
flow channel
furnace
tunnel furnace
secondary firing
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
JP63239974A
Other languages
Japanese (ja)
Other versions
JP2704736B2 (en
Inventor
Masahisa Mimoji
三文字 昌久
Teruo Kamimura
上村 照夫
Hitoshi Hiroi
広井 均
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.)
Tokai Carbon Co Ltd
Original Assignee
Tokai Carbon Co 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 Tokai Carbon Co Ltd filed Critical Tokai Carbon Co Ltd
Priority to JP63239974A priority Critical patent/JP2704736B2/en
Priority to CN 89103061 priority patent/CN1041443A/en
Publication of JPH0289988A publication Critical patent/JPH0289988A/en
Application granted granted Critical
Publication of JP2704736B2 publication Critical patent/JP2704736B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Carbon And Carbon Compounds (AREA)
  • Tunnel Furnaces (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Abstract] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は、人造黒鉛電極などを製造する過程において、
ピッチ浸透した黒鉛素材を二次的に焼成する目的に存効
なトンネル炉に関する。
[Detailed Description of the Invention] (Industrial Application Field) The present invention provides a method for manufacturing artificial graphite electrodes, etc.
This invention relates to a tunnel furnace that is effective for secondary firing of pitch-infiltrated graphite material.

〔従来の技術〕[Conventional technology]

ピッチ浸透した黒鉛素材のトンネル炉焼成は、処理すべ
き黒鉛素材を台車上に覆設したサガー内に搭載し、台車
を予熱帯域、焼成帯域および冷却帯域からなるトンネル
炉中を順次送行させることによっておこなわれる。この
処理中、浸透材として黒鉛素材の内部に浸入したピッチ
成分は、予熱帯域において融点以上の受熱作用を受けて
多量に溶出する。ピッチ成分の溶出度合は、とくにバッ
キングレス構造の台車を使用する場合に激しく起り、こ
れが気液状態でサガー外部に漏出して炉内事故あるいは
公害化現象をもたらす原因となっている。
Tunnel furnace firing of pitch-infiltrated graphite material is carried out by loading the graphite material to be treated in a sagger covered by a cart, and moving the cart sequentially through the tunnel furnace, which consists of a preheating zone, a firing zone, and a cooling zone. It is carried out. During this treatment, the pitch component that has entered the inside of the graphite material as a penetrating agent is eluted in large quantities by receiving heat at a temperature higher than the melting point in the preheating zone. The degree of elution of the pitch component is particularly severe when a backingless structure truck is used, and this leaks out of the sagger in a gas-liquid state, causing accidents in the furnace or pollution phenomena.

これらの欠点を解消するため、浸透素材から流出したタ
ール・ピッチを台車の台座に設けたタール・ピッチ流出
穴を通してビット内の水中に没設されるコンベヤに流下
させてトンネルキルンの燃焼ゾーンから系外に取り出し
て焼成するトンネルキルンによる炭素材焼成法が提案さ
れている(特公昭60−29642号公報)。
To overcome these drawbacks, the tar pitch escaping from the permeable material is transported from the combustion zone of the tunnel kiln to the system by flowing it down through a tar pitch outflow hole in the base of the trolley to a conveyor submerged in water inside the bit. A carbon material firing method using a tunnel kiln in which the carbon material is taken outside and fired has been proposed (Japanese Patent Publication No. 60-29642).

(発明が解決しようとするi!1fl)しかしながら、
前記特公昭60−29642号の発明による場合にはコ
ンヘンヤ機構をビット内の水中に没設する必要があるた
め、駆動部分を含むコンベンヤ部材が炉内の7g循環条
件を受けて短時間内に劣化を貝傷する現象が生じる。し
たがって、安全な操業をおこなうためには、頻繁にコン
ベンヤ機構の点検補修を実施しなければならない実用上
の問題点があった。
(i!1fl that the invention tries to solve) However,
In the case of the invention disclosed in Japanese Patent Publication No. 60-29642, it is necessary to immerse the conveyor mechanism in water inside the bit, so the conveyor member including the driving part deteriorates within a short period of time due to the 7g circulation conditions in the furnace. The phenomenon of shellfish scratches occurs. Therefore, there is a practical problem in that the conveyor mechanism must be frequently inspected and repaired in order to operate safely.

本発明は、系内に機械的な運搬機構を付設することなし
に、溶出してサガー内部を流下する液状のピッチ成分を
円滑に系外に導出して分離捕集することができる聞易構
造のトンネル炉を提供するものである。
The present invention has an easy-to-understand structure that allows liquid pitch components eluted and flowing down the sagger to be smoothly led out of the system and separated and collected without installing a mechanical transport mechanism inside the system. This is a tunnel furnace.

(課題を解決するための手段) すなわち、本発明に係る黒鉛素材二次焼成用トンネル炉
は、台車のピッチ流出ノズル直下に位1する炉床の少く
とも予熱帯域に相当する炉長範囲に、傾斜面を有する凹
状流水路を敷設し、該凹状流水路を連続的に流水する構
造からなるものである。
(Means for Solving the Problem) That is, the tunnel furnace for secondary firing of graphite material according to the present invention has a furnace length range corresponding to at least the preheating zone of the hearth located directly below the pitch outflow nozzle of the cart. It consists of a structure in which a concave flow channel with an inclined surface is laid and water flows continuously through the concave flow channel.

上記の構造において、凹状流水路の傾斜下端部をピッチ
捕集受槽に連通させ、ポンプを介して前記ピッチ捕集受
槽と凹状流水路の傾斜上端部とを流水管で連結すること
により流水I!経路を構成しておくと一層円滑に捕集回
収をおこなうことができる。
In the above structure, the sloped lower end of the concave flow channel is communicated with the pitch collecting tank, and the pitch collecting tank and the sloped upper end of the concave flow channel are connected by a water pipe via a pump, thereby allowing flowing water to flow I! By configuring a route, collection and collection can be carried out even more smoothly.

〔作 用] トンネル炉を送行中に発生した液状のピッチ成分は、台
車のピッチ流出ノズルを経て凹状流水路の流水中に落下
する。落下時、ピッチ成分は滴状に分断されて流水と接
触し、凝固しながら流水に同伴して移送される。この間
にピッチ成分は流動ならびに凝縮作用を受けて急速に直
径1〜5II11程度の球形に造粒される。したがって
、その後は小球状ピッチの状態により凹状流水路の傾斜
面に沿って自然に自己転勤し、自動的に捕集系統に流排
出される。
[Function] The liquid pitch component generated during transport through the tunnel furnace passes through the pitch outflow nozzle of the truck and falls into the flowing water of the concave flow channel. When falling, the pitch component is broken into droplets, contacts the flowing water, and is transported along with the flowing water while solidifying. During this time, the pitch component is subjected to flow and condensation action and is rapidly granulated into spherical particles having a diameter of about 1 to 5II11. Therefore, after that, depending on the state of the small spherical pitch, the particles naturally self-translocate along the slope of the concave flow channel and are automatically discharged to the collection system.

〔実施例〕〔Example〕

以下、本発明を図示した一実施例に基づいて説明する。 The present invention will be described below based on an illustrated embodiment.

第1図は、本発明に係るトンネル炉の縦断面略図、第2
図は炉の予熱IFMを示す横断面図である。
FIG. 1 is a schematic vertical cross-sectional view of a tunnel furnace according to the present invention, and FIG.
The figure is a cross-sectional view showing the preheating IFM of the furnace.

図中、lは炉壁、2は連結状態で炉内を送行する台車で
ある0台車2は、上部にガス排出孔3を有するサガー4
を、黒鉛素材5を搭載した受皿6を介して台座7上に覆
設した構造がらなり、スカート板8を炉壁の摺動サンド
シール装置9に挿入して台座上下の雰囲気を遮断した状
態で軌道10上を走行する。受皿および台座7には、中
央位置にそれぞれ連通する1個ないし複数個のピッチ流
出ノズル11.11’が付設されている。
In the figure, l is the furnace wall, 2 is a truck that moves through the furnace in a connected state, and 0 truck 2 is a sagger 4 having a gas discharge hole 3 at the top.
is covered on a pedestal 7 via a saucer 6 loaded with graphite material 5, and a skirt plate 8 is inserted into a sliding sand seal device 9 on the furnace wall to block the atmosphere above and below the pedestal. Travels on track 10. The saucer and the base 7 are provided with one or more pitch outflow nozzles 11.11' each communicating with a central position.

工2は炉天井部に設けたガス導出口で、炉上の排ガス吸
引ダクト13に連結する。
The pipe 2 is a gas outlet provided in the ceiling of the furnace, and is connected to the exhaust gas suction duct 13 above the furnace.

14は、台車のピッチ流出ノズル11’直下に位置する
炉床に敷設された凹状流水路で、少くともピッチ溶出が
著しい予熱帯域に相当する炉長範囲に流水可能な傾斜面
をもたせて設置する。傾斜形状は、第1図に例示したV
型傾斜のほか、一方傾斜に設計することもできる。該凹
状流水路14は、炉床にビット溝として掘設するか、適
宜な金属材料で製作した樋を付設することにより形成さ
れる。
14 is a concave flow channel laid in the hearth located directly below the pitch outflow nozzle 11' of the cart, and is installed with an inclined surface that allows water to flow at least in the furnace length range corresponding to the preheating zone where pitch elution is significant. . The inclined shape is V as shown in FIG.
In addition to the mold tilt, it can also be designed to have a one-sided tilt. The concave flow channel 14 is formed by digging a bit groove in the hearth or by attaching a gutter made of a suitable metal material.

炉運転にあたり、凹状流水路14に連続的に水を流す、
ブツシャ−装置により予熱帯域に送入された台車2は加
熱作用を受け、搭載した処理黒鉛素材からピッチ成分の
溶出がはじまる。溶出ピッチ成分は受皿6面に流下し、
一部は気化してサゴ−4上部のガス排出孔3からガス導
出口12を経て、排ガスダクト】3により適宜な処理装
置に至る。
When operating the furnace, water is continuously allowed to flow through the concave flow channel 14.
The cart 2 sent into the preheating zone by the butcher device is heated, and pitch components begin to be eluted from the treated graphite material loaded thereon. The eluted pitch component flows down to the 6 sides of the saucer,
A part of the gas is vaporized and passes through the gas outlet 12 from the gas exhaust hole 3 in the upper part of the sago 4, and reaches an appropriate processing device through the exhaust gas duct 3.

受皿6に溜まった液状のピッチ成分は、台車のピッチ流
出ノズル11′を経て凹状流水fl14の流水中に落下
する。N工時、ピッチ成分は滴状に分断されて流水と接
触し、凝固しながら流水に同伴して移送する。この間に
ピッチ成分は流動作用により直径1〜5m+w程度の球
形に造粒され、凹状流水路14を1頃斜面に沿って自然
に転勤する。
The liquid pitch component accumulated in the saucer 6 passes through the pitch outflow nozzle 11' of the truck and falls into the flowing water of the concave flowing water fl14. During the N process, the pitch component is broken into droplets, comes into contact with running water, and is transported along with the running water while solidifying. During this time, the pitch component is granulated into a spherical shape with a diameter of about 1 to 5 m+w by the flow action, and is naturally transferred along the slope of the concave flow channel 14 at around 1.

ピッチ溶出現象は、台車が予熱帯中央部にさしかかった
時点で最高となり、−時に多量の液状ビッチを流出する
が、流水による炉底部の冷却効果と相俟って、流下する
液状ピッチが気化することなく極めて円滑に上記流排出
が進行する。この状態は、ピッチ成分の溶出が完結する
予熱帯域の終点に至るまで継続する。
The pitch elution phenomenon reaches its peak when the cart approaches the center of the preheating zone, and sometimes a large amount of liquid pitch flows out, but together with the cooling effect of the bottom of the reactor by running water, the flowing liquid pitch vaporizes. The above-mentioned flow discharge progresses extremely smoothly without any problems. This state continues until the end of the preheating zone, where the elution of the pitch component is completed.

固形化した球形ピッチを伴った流水はピッチ捕集受槽I
5に入り、固液分離操作によりピッチ成分を分離捕集す
る0回収したピッチは、浸透材あるいは燃料として再利
用される。
Flowing water with solidified spherical pitch is sent to pitch collecting tank I.
5, the pitch components are separated and collected by a solid-liquid separation operation.The recovered pitch is reused as a penetrating material or fuel.

流水循環経路を構成する場合には、固液分離後の水をポ
ンプ16により汲み上げ、凹状流水路14の傾斜上端部
に連通ずる流水管17に還元する。この回路機構により
流水は連続的に循環して円滑にピッチ流排出を進行させ
ることができる。
When constructing a flowing water circulation path, the water after solid-liquid separation is pumped up by the pump 16 and returned to the flowing water pipe 17 communicating with the inclined upper end of the concave water channel 14. With this circuit mechanism, the water can be continuously circulated and pitch flow discharge can proceed smoothly.

このようにして、ピッチ溶出が完結した台車は、引続き
焼成帯域に進行して焼成処理を受け、さらに冷却帯域を
経て操業を完了する。
In this manner, the cart whose pitch elution has been completed continues to the firing zone where it undergoes firing treatment, and further passes through the cooling zone to complete its operation.

(発明の効果〕 本発明によれば、コンベヤ等の機械的運搬機構のない簡
易な炉構造により台車下部に流出する液状ピッチ成分を
完全に回収することができるから、煩雑な点検補修をお
こなうことなしに常に安全かつ円滑な炉運転が保障され
る。そのうえ、回収したピッチ成分は浸透材あるいは燃
料として再利用できるから、公害防止および原価削減の
面からも実用的効果をもたらす利益がある。
(Effects of the Invention) According to the present invention, the liquid pitch component flowing out to the bottom of the cart can be completely recovered using a simple furnace structure without a mechanical conveyance mechanism such as a conveyor, thereby eliminating the need for complicated inspection and repair. Safe and smooth furnace operation is guaranteed at all times.Furthermore, since the recovered pitch component can be reused as a penetrant or fuel, there are practical benefits in terms of pollution prevention and cost reduction.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明に係るトンネル炉構造を例示した縦断面
略図、第2図は炉の予熱帯域を示した横断面図である。 l・・・炉壁、      2・・・台車、3・・・ガ
ス排出孔、  4・・・サガー5・・・黒鉛素材、  
 6・・・受皿、7・・・台座、      8・・・
スカート板、9・・・摺動サンドシール装置、 IO・
・・軌道、11・・・ピッチ流出ノズル、 12・・・
ガス導出口、13・・・排ガス吸引ダクト、 14・・
・凹状流水路、15・・・ピッチ捕集受槽、  16・
・・ポンプ、17・・・流水管。
FIG. 1 is a schematic vertical cross-sectional view illustrating a tunnel furnace structure according to the present invention, and FIG. 2 is a cross-sectional view showing a preheating zone of the furnace. l...furnace wall, 2...carriage, 3...gas discharge hole, 4...sagger 5...graphite material,
6... saucer, 7... pedestal, 8...
Skirt plate, 9...Sliding sand seal device, IO・
...Trajectory, 11...Pitch outflow nozzle, 12...
Gas outlet, 13...Exhaust gas suction duct, 14...
・Concave flow channel, 15... Pitch collection tank, 16.
... Pump, 17... Water pipe.

Claims (1)

【特許請求の範囲】 1、台車のピッチ流出ノズル(11′)直下に位置する
炉床の少くとも予熱帯域に相当する炉長範囲に、傾斜面
を有する凹状流水路(14)を敷設し、該凹状流水路を
連続的に流水する構造の黒鉛素材二次焼成用トンネル炉
。 2、凹状流水路(14)の傾斜下端部がピッチ捕集受槽
(15)に連通し、ポンプ(16)を介して前記ピッチ
捕集受槽と凹状流水路の傾斜上端部とを流水管で連結す
ることにより流水循環経路を構成する請求項1記載の黒
鉛素材二次焼成用トンネル炉。
[Claims] 1. A concave flow channel (14) having an inclined surface is laid in the furnace length range corresponding to at least the preheating zone of the hearth located directly below the pitch outflow nozzle (11') of the truck, A tunnel furnace for secondary firing of graphite material having a structure in which water continuously flows through the concave flow channel. 2. The sloped lower end of the concave flow channel (14) communicates with the pitch collection tank (15), and the pitch collection tank and the sloped upper end of the concave flow channel are connected by a water pipe via a pump (16). 2. The tunnel furnace for secondary firing of graphite material according to claim 1, wherein the tunnel furnace for secondary firing of graphite material comprises a running water circulation path.
JP63239974A 1988-09-26 1988-09-26 Tunnel furnace for secondary firing of graphite material Expired - Fee Related JP2704736B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP63239974A JP2704736B2 (en) 1988-09-26 1988-09-26 Tunnel furnace for secondary firing of graphite material
CN 89103061 CN1041443A (en) 1988-09-26 1989-05-06 Tunnel Furnaces for Manufacture of Artificial Graphite Electrodes

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP63239974A JP2704736B2 (en) 1988-09-26 1988-09-26 Tunnel furnace for secondary firing of graphite material

Publications (2)

Publication Number Publication Date
JPH0289988A true JPH0289988A (en) 1990-03-29
JP2704736B2 JP2704736B2 (en) 1998-01-26

Family

ID=17052600

Family Applications (1)

Application Number Title Priority Date Filing Date
JP63239974A Expired - Fee Related JP2704736B2 (en) 1988-09-26 1988-09-26 Tunnel furnace for secondary firing of graphite material

Country Status (2)

Country Link
JP (1) JP2704736B2 (en)
CN (1) CN1041443A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6446157A (en) * 1987-08-14 1989-02-20 Shaken Kk Production system for ruled line table
WO2005096501A1 (en) * 2004-04-02 2005-10-13 Kaben Research Inc. Phase frequency detector with a novel d flip flop
CN116576685A (en) * 2023-06-14 2023-08-11 宣城鸿海装备科技有限公司 An exhaust device for the replacement chamber of an atmosphere roller furnace

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4740715B2 (en) * 2004-10-21 2011-08-03 新日鐵化学株式会社 Carbon material firing furnace and carbon material firing method
EP2909555B1 (en) * 2012-10-16 2018-05-23 Lazar Anode Technologies AG Carbon baking furnace
CN110655055A (en) * 2018-06-29 2020-01-07 山西贝特瑞新能源科技有限公司 Continuous carbide furnace device of negative electrode material
CN113999010B (en) * 2021-12-14 2023-03-28 中钢集团南京新材料研究院有限公司 Preparation method of high-performance special graphite

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6446157A (en) * 1987-08-14 1989-02-20 Shaken Kk Production system for ruled line table
WO2005096501A1 (en) * 2004-04-02 2005-10-13 Kaben Research Inc. Phase frequency detector with a novel d flip flop
CN116576685A (en) * 2023-06-14 2023-08-11 宣城鸿海装备科技有限公司 An exhaust device for the replacement chamber of an atmosphere roller furnace

Also Published As

Publication number Publication date
CN1041443A (en) 1990-04-18
JP2704736B2 (en) 1998-01-26

Similar Documents

Publication Publication Date Title
KR100666809B1 (en) Direct smelting vessel
US9663837B2 (en) Device for recovering heat and fumes from slag resulting from the steel production cycle
KR101349238B1 (en) Direct smelting plant
US8097065B2 (en) System and method for producing metallic iron
CA2665562C (en) System and method of producing metallic iron
US4046541A (en) Slag quenching method for pyrolysis furnaces
KR20010095028A (en) Temperature control device and temperature control method for high-temperature exhaust gas
US3460818A (en) Apparatus for treatment of particulate material on moving support
JPH0289988A (en) Tunnel furnace for secondary firing of graphite materials
CN1191376C (en) Directly smelting apparatus
US3947001A (en) Combustion system
US3315443A (en) Method and apparatus for cleaning exhaust gases from oxygen steelmaking furnaces
JPH09316562A (en) Dry type smelting method of copper
US5013336A (en) Method and apparatus for emission control
KR920000517B1 (en) Slag treatment method and apparatus
JP2000226618A (en) Waste heat recovery method for sinter cooler and sinter cooler
US4856987A (en) Tunnel kiln for ceramic firing
BRPI0409281B1 (en) DIRECT REDUCTION INSTALLATION TO PRODUCE CAST METAL FROM METAL FEED MATERIAL
US4082252A (en) Method and system for processing molten slag
US4255131A (en) Apparatus and method for heating an aggregate material
KR20110113223A (en) Method of manufacturing iron ingots using plasma
FI111028B (en) Process for cooling a gas flow from a furnace
EP0176536B1 (en) Apparatus for and a method of removing material
SU1528755A1 (en) Installation for processing slag melt
CN1934278A (en) Direct smelting plant

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees