JPS6248530B2 - - Google Patents

Info

Publication number
JPS6248530B2
JPS6248530B2 JP58046327A JP4632783A JPS6248530B2 JP S6248530 B2 JPS6248530 B2 JP S6248530B2 JP 58046327 A JP58046327 A JP 58046327A JP 4632783 A JP4632783 A JP 4632783A JP S6248530 B2 JPS6248530 B2 JP S6248530B2
Authority
JP
Japan
Prior art keywords
powder
rotary valve
cooling furnace
discharge
vertical cooling
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.)
Expired
Application number
JP58046327A
Other languages
Japanese (ja)
Other versions
JPS59173128A (en
Inventor
Juzo Terai
Masatoshi Kobayashi
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.)
Nippon Steel Corp
Original Assignee
Nippon Steel Corp
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 Nippon Steel Corp filed Critical Nippon Steel Corp
Priority to JP4632783A priority Critical patent/JPS59173128A/en
Publication of JPS59173128A publication Critical patent/JPS59173128A/en
Publication of JPS6248530B2 publication Critical patent/JPS6248530B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/0015Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
    • B01J8/002Feeding of the particles in the reactor; Evacuation of the particles out of the reactor with a moving instrument

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Coke Industry (AREA)
  • Vertical, Hearth, Or Arc Furnaces (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は気密を要する粉粒体用竪型式冷却炉の
粉粒体排出装置に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a powder discharge device for a vertical cooling furnace for powder and granule which requires airtightness.

〔従来の技術及び問題点〕[Conventional technology and problems]

気密を要する粉粒体用竪型式冷却炉の排出装置
としては、例えば、コークス乾式消火設備の竪型
式冷却炉から冷却されたコークスを排出する排出
装置がある。これらの設備においては、装置高さ
を低減することが設備コストダウン上重要である
が、従来、ソ連ギプロコークスの例の如く、竪型
式冷却炉の底部よりカツトゲートを介してコーク
スをバツチ式で切出し、2重のシール弁を持つシ
ールホツパーで気密し、一旦コークワーフに卸し
た後ワーフゲートにて、払出ベルトコンベヤーに
連続排出を行なつているため、排出装置全体の高
さが大きくなることは避けられなかつた。
An example of a discharge device for a vertical cooling furnace for powder and granular materials that requires airtightness is a discharge device for discharging cooled coke from a vertical cooling furnace of a coke dry extinguishing facility. In these facilities, reducing the height of the equipment is important in terms of reducing equipment costs. Conventionally, coke was cut out in batches from the bottom of a vertical cooling furnace through a cut gate, as was the case with the Soviet Union's Gipro coke. The material is airtight using a seal hopper with a double seal valve, and after being unloaded to Cork Wharf, it is continuously discharged to a delivery belt conveyor at a wharf gate, so it was unavoidable that the overall height of the discharge device would be large. .

又、特開昭57−36184号では、竪型式冷却炉よ
り連続切出しを行なう方式が提案されているが、
該方式も気密手段はやはり、2重のシール弁を持
つシールホツパーによつているため排出装置の高
さが高くなることには変りない。
Furthermore, in Japanese Patent Application Laid-open No. 57-36184, a method of continuous cutting from a vertical cooling furnace is proposed.
In this method, the airtight means still relies on a seal hopper having a double seal valve, so the height of the discharge device remains high.

さらに、第1図に示す如く、竪型式冷却炉2の
粉粒体出口5に直接ロータリー弁1を臨ませて用
いる方式が知られているが、コークスの不所望な
かみ込みによる破砕、負荷の増大及びローター
3、ケーシング4に著しい摩耗が生じ、気密機能
は短時間の運転で保障されなくなる欠点があるた
め、実用化は困難である。
Furthermore, as shown in Fig. 1, a method is known in which a rotary valve 1 is placed directly facing the powder outlet 5 of a vertical cooling furnace 2, but this method causes crushing due to undesired coke entrainment, and reduces the load. It is difficult to put it into practical use because of the disadvantages that the rotor 3 and casing 4 are subject to significant wear and the airtight function is no longer guaranteed after a short period of operation.

本発明は前述の問題を解決し、気密を保ちなが
ら粉粒体を連続的に排出でき、しかも設備全体の
高さを低くすることにより安価な排出装置を提供
せんとするものである。
The present invention solves the above-mentioned problems and provides an inexpensive discharge device that can continuously discharge powder and granular materials while maintaining airtightness, and further reduces the height of the entire equipment.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は、粉粒体用竪型式冷却炉の排出装置に
おいて、前記竪型式冷却炉の粉粒体出口の下部
に、粉粒体を連続的且つ定量的に送り出す形式の
搬送装置を設けると共に、該搬送装置の排出部に
ロータリー弁を設け、前記冷却炉の粉粒体出口と
ロータリー弁の入口を連通し且つ前記搬送装置を
外気と隔絶する如く形成した気密室を設けると共
にローター回転方向に面したロータリー弁供給口
のシユート壁とロータリー弁ケーシング外周部と
の接合部が粉粒体落下軌跡より遠方に位置する如
く形成し、ロータリー弁排出口を水平近傍から開
口させ、更に前記搬送装置はロータリー弁の粉粒
体切出能力より少ない供給量に制御可能に構成し
たことを特徴とする粉粒体用竪型式冷却炉の排出
装置である。
The present invention provides a discharging device for a vertical cooling furnace for powder and granular materials, in which a conveying device for continuously and quantitatively feeding out the powder and granules is provided below the powder outlet of the vertical cooling furnace, and A rotary valve is provided at the discharge section of the conveying device, and an airtight chamber is provided which communicates the powder outlet of the cooling furnace with the inlet of the rotary valve and isolates the conveying device from the outside air. The joint between the chute wall of the rotary valve supply port and the outer periphery of the rotary valve casing is formed so as to be located far from the falling locus of the powder and granular material, and the rotary valve discharge port is opened from near horizontally. This is a discharge device for a vertical cooling furnace for powder and granular material, characterized in that it is configured to be able to control the supply amount to be smaller than the powder and granular material cutting capacity of a valve.

〔実施例〕〔Example〕

以下本発明の実施例を図面に基づいて説明す
る。
Embodiments of the present invention will be described below based on the drawings.

第2図は竪型式冷却炉2の粉粒体出口下部の気
密室6内に搬送装置である振動フイーダー7を設
け、該振動フイーダー7の排出部にロータリー弁
1を設けた例である。図において、3はロータ
ー、4はケーシング、8はローターの羽根であ
る。
FIG. 2 shows an example in which a vibrating feeder 7, which is a conveying device, is provided in an airtight chamber 6 at the lower part of the powder outlet of a vertical cooling furnace 2, and a rotary valve 1 is provided at the discharge portion of the vibrating feeder 7. In the figure, 3 is a rotor, 4 is a casing, and 8 is a blade of the rotor.

ローター3は、第3図に示すように、側板9を
設けたものがよく、振動フイーダー7より定量的
に切出された粉粒体はロータリー弁1の供給口5
に供給され、さらにロータリー弁1から排出され
て払出ベルトコンベヤー13で運搬される。
The rotor 3 is preferably provided with a side plate 9, as shown in FIG.
It is further discharged from the rotary valve 1 and conveyed by a delivery belt conveyor 13.

振動フイーダー7は、特に大きな粒度(200mm
以上)以外は、定量切出性は良好であるため、ロ
ーターの羽根8と側板9とで構成される各空間
(部屋)に収容能力を超えて供給することが無い
ように、即ち、満杯とならないように供給量を制
御して粒状物を入れることが可能である。また振
動フイーダー7をロータリー弁1の上流側に設け
たことにより、ロータリー弁1の供給口5の開口
幅aに対し粒状物の落下流量幅bを小さく取るこ
とが可能となる。又ローター回転方向に面したロ
ータリー弁供給口のシユート壁14とロータリー
弁のケーシング4外周部との接合部を粉粒体落下
軌跡より遠方に位置させることによりローターの
羽根8とケーシング4との間への粉粒体のかみこ
みを防止できる。
The vibrating feeder 7 has a particularly large grain size (200mm
Other than the above), the quantitative cutting performance is good, so it is necessary to ensure that each space (room) consisting of the rotor blades 8 and side plate 9 is not supplied in excess of its capacity. It is possible to introduce granules by controlling the feed rate to avoid Further, by providing the vibrating feeder 7 on the upstream side of the rotary valve 1, it is possible to make the falling flow rate width b of the particulate matter smaller than the opening width a of the supply port 5 of the rotary valve 1. In addition, by locating the joint between the rotary valve supply port's chute wall 14 facing the rotor rotation direction and the outer periphery of the rotary valve's casing 4 at a distance from the falling locus of the powder and granules, the gap between the rotor blades 8 and the casing 4 is increased. This prevents powder and granules from getting caught in the container.

又、供給口5において粉粒体の落下流にさらさ
れるローターの羽根8の先端部の摩耗が問題とな
るが、振動フイーダー7によつてロータリー弁1
の供給口5に供給される粉粒体の落下速度を最小
にできるため、ソフトに供給でき、ローターの羽
根8先端部の摩耗条件を有利にできる。しかもこ
の部分の摩耗は局部的であり、高Cr鋳鉄製等の
耐摩材を使用しても、ロータリー弁1全体の設備
費用には、問題とならない。高圧の気密性が要求
される場合には、窒化硅素セラミツクの如く、超
耐摩耗材をこの部分に採用するか、あるいは、取
替構造とし、定期的に取替るようにして高度の気
密性を維持できる。
In addition, wear of the tips of the rotor blades 8 exposed to the falling flow of powder and granules at the supply port 5 poses a problem.
Since the falling speed of the powder and granular material supplied to the supply port 5 can be minimized, the powder can be supplied softly, and the wear conditions at the tips of the blades 8 of the rotor can be made favorable. Moreover, the wear in this part is local, and even if a wear-resistant material such as high Cr cast iron is used, the equipment cost of the rotary valve 1 as a whole does not pose a problem. If high-pressure airtightness is required, a super wear-resistant material such as silicon nitride ceramic should be used for this part, or a replacement structure should be used and replaced periodically to maintain a high degree of airtightness. can.

又、ロータリー弁の排出口15はケーシング4
が粉粒体の接触及び回転による摩耗の無きよう水
平近傍から開口させる。こうすればローター内に
充填された粉粒体がケーシングと接触することな
く排出されるので、粉粒体によるケーシングの摩
耗が無くなり、メンテナンス頻度を低減すること
ができる。なおロータリー弁の機密性の向上を考
慮すればケーシング外周部は可能な限り長くした
方が良いことから開口の開始点をC点より上げて
はならない。
Also, the discharge port 15 of the rotary valve is connected to the casing 4.
The opening is made near the horizontal to avoid wear due to contact and rotation of the powder and granules. In this way, the powder filled in the rotor is discharged without coming into contact with the casing, thereby eliminating wear on the casing due to the powder and reducing the frequency of maintenance. Note that in consideration of improving the airtightness of the rotary valve, it is better to make the outer periphery of the casing as long as possible, so the starting point of the opening should not be raised above point C.

更に振動フイーダー7は価格も安価で、耐久性
も十分あり実用性が高い。特に定量切出装置とし
てコンパクトな点は、本発明にとつて重要であ
り、排出装置のみならず冷却炉全体を低くできる
ので設備費が低減される。
Furthermore, the vibration feeder 7 is inexpensive, sufficiently durable, and highly practical. Particularly, the compactness of the quantitative cut-out device is important for the present invention, and not only the discharge device but also the entire cooling furnace can be made low-profile, which reduces equipment costs.

本発明の他の実施例としてエプロンフイーダー
をロータリー弁の上流側に定量切出装置として利
用する例を第4図に示す。
Another embodiment of the present invention is shown in FIG. 4, in which an apron feeder is used as a quantitative cutting device upstream of a rotary valve.

図において、10はエプロンフイーダーで、他
の符号は前記実施例の第2図のものと同一のもの
を指す。
In the figure, 10 is an apron feeder, and other symbols refer to the same parts as in FIG. 2 of the above embodiment.

エプロンフイーダー10の特徴は、大粒度の粉
粒体の切出に対しても定量切出性がすぐれてお
り、定量切出性という点では最もすぐれている
が、本発明におけるロータリー弁1との組み合せ
においては、供給される粉粒体の流量巾bを絞る
ために小さなシユート11を設け、ロータリー弁
1での粉粒体のかみ込みを防止することが好まし
い。
The feature of the apron feeder 10 is that it has excellent quantitative cutting performance even when cutting out large-sized powder particles, and is the most excellent in terms of quantitative cutting performance. In this combination, it is preferable to provide a small chute 11 in order to narrow down the flow width b of the supplied powder and granule to prevent the rotary valve 1 from getting caught in the powder and granule.

さらに他の実施例としてロールフイーダーをロ
ータリー弁の上流側に定量切出装置として利用す
る例を第5図に示す。
As yet another embodiment, an example in which a roll feeder is used as a quantitative cutting device upstream of a rotary valve is shown in FIG.

図において、12はロールフイーダーで、他の
符号は前記実施例の第3図、第4図のものと同一
のものを指す。
In the figure, 12 is a roll feeder, and the other symbols refer to the same parts as in FIGS. 3 and 4 of the above embodiment.

ロールフイーダー12の特徴は、構造が簡単
で、耐久性にすぐれ、安価である点である。また
前記エプロンフイーダーとロータリー弁との組合
せの場合と同様にロータリー弁1での粉粒体のか
み込みを防止するため、ロールフイーダー12の
排出部に小さなシユート11を設けた方がよい。
The roll feeder 12 is characterized by its simple structure, excellent durability, and low cost. Further, as in the case of the combination of the apron feeder and the rotary valve, it is preferable to provide a small chute 11 at the discharge portion of the roll feeder 12 in order to prevent the powder from being caught in the rotary valve 1.

〔発明の効果〕〔Effect of the invention〕

以上説明したように構成される本発明によれば
以下の効果がある。
The present invention configured as described above has the following effects.

竪型式冷却炉の気密を保ちながら粉粒体を連
続的に排出できるので、コークワーフやシール
ホツパー等、粉粒体を一時的に貯蔵する設備が
不要である。
Since the powder and granules can be continuously discharged while maintaining the airtightness of the vertical cooling furnace, there is no need for equipment to temporarily store the powder and granules, such as a coke wharf or a seal hopper.

又、竪型式冷却炉の気密を保つのに二重シー
ル弁を使わずに、ロータリー弁を使用するた
め、排出装置の装置高が低くなる。従つて竪型
式冷却炉の設備全体が低くなり設備費が低減さ
れる。
Furthermore, since a rotary valve is used instead of a double seal valve to maintain the airtightness of the vertical cooling furnace, the height of the discharge device is reduced. Therefore, the overall cost of the equipment for the vertical cooling furnace is reduced.

ロータリー弁供給口のローター回転方向に面
したシユート壁とロータリー弁ケーシング外周
部との接合部を粉粒体落下軌跡より遠方に位置
させたので、ローター羽根とケーシングとの間
に粉粒体をかみ込むことが無くなる。
The joint between the rotary valve supply port's chute wall facing the rotor rotational direction and the outer periphery of the rotary valve casing is located far away from the falling trajectory of the powder and granules, so that the powder and granules are caught between the rotor blades and the casing. You won't have to worry about it.

粉粒体がローターに満杯にならないように
し、且つロータリー弁排出口を水平近傍から開
口させることにより、粉粒体がケーシング内面
に接触することが無いのでケーシング内面の摩
耗が無くなる。
By preventing the rotor from being filled with powder and granules and by opening the rotary valve outlet near the horizontal, the powder does not come into contact with the inner surface of the casing, thereby eliminating wear on the inner surface of the casing.

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

第1図は粉粒体用竪型式冷却炉の底部にロータ
リー弁を設置した従来方式の例を示す断面説明
図、第2図は粉粒体用竪型式冷却炉の底部に振動
フイーダーを設け、振動フイーダーの排出部にロ
ータリー弁を設けた本発明の実施例を示す断面説
明図、第3図は本発明に使用するロータリー弁の
ローターの斜視図、第4図は粉粒体用竪型式冷却
炉の底部にエプロンフイーダーを設け、エプロン
フイーダーの排出部にロータリー弁を設けた本発
明の実施例を示す断面説明図、第5図は粉粒体用
竪型式冷却炉の底部にロールフイーダーを設け、
ロールフイーダーの排出部にロータリー弁を設け
た本発明の実施例を示す断面説明図である。 1……ロータリー弁、2……竪型式冷却炉、3
……ロータリー弁のローター、4……ロータリー
弁のケーシング、5……ロータリー弁の供給口、
6……気密室、7……振動フイーダー、8……ロ
ーターの羽根、9……ローターの側板、10……
エプロンフイーダー、11……シユート、12…
…ロールフイーダー、13……払出ベルトコンベ
ヤー、14……ローター回転方向に面したロータ
リー弁供給口のシユート壁、15……ロータリー
弁の排出口。
Figure 1 is a cross-sectional explanatory diagram showing an example of a conventional method in which a rotary valve is installed at the bottom of a vertical cooling furnace for powder and granular materials, and Figure 2 is a vibrating feeder installed at the bottom of a vertical cooling furnace for powder and granular materials. A cross-sectional explanatory diagram showing an embodiment of the present invention in which a rotary valve is provided in the discharge section of a vibrating feeder, FIG. 3 is a perspective view of the rotor of the rotary valve used in the present invention, and FIG. 4 is a vertical type cooling for powder and granular materials. A cross-sectional explanatory view showing an embodiment of the present invention in which an apron feeder is provided at the bottom of the furnace and a rotary valve is provided at the discharge part of the apron feeder. Established Ida;
FIG. 2 is an explanatory cross-sectional view showing an embodiment of the present invention in which a rotary valve is provided in the discharge section of the roll feeder. 1... Rotary valve, 2... Vertical cooling furnace, 3
... rotor of rotary valve, 4 ... casing of rotary valve, 5 ... supply port of rotary valve,
6... Airtight chamber, 7... Vibration feeder, 8... Rotor blade, 9... Rotor side plate, 10...
Apron feeder, 11... Shoot, 12...
...roll feeder, 13...discharge belt conveyor, 14...chute wall of rotary valve supply port facing the rotor rotation direction, 15... rotary valve discharge port.

Claims (1)

【特許請求の範囲】[Claims] 1 粉粒体用竪型式冷却炉の排出装置において、
前記竪型式冷却炉の粉粒体出口の下部に、粉粒体
を連続的且つ定量的に送り出す形式の搬送装置を
設けると共に、該搬送装置の排出部にロータリー
弁を設け、前記冷却炉の粉粒体出口とロータリー
弁の入口を連通し且つ前記搬送装置を外気と隔絶
する如く形成した気密室を設けると共にローター
回転方向に面したロータリー弁供給口のシユート
壁とロータリー弁ケーシング外周部との接合部が
粉粒体落下軌跡より遠方に位置する如く形成し、
ロータリー弁排出口を水平近傍から開口させ、更
に前記搬送装置はロータリー弁の粉粒体切出能力
より少ない供給量に制御可能に構成したことを特
徴とする粉粒体用竪型式冷却炉の排出装置。
1. In the discharge device of a vertical cooling furnace for powder and granular materials,
A conveying device for continuously and quantitatively feeding out the powder and granules is provided below the powder outlet of the vertical cooling furnace, and a rotary valve is provided at the discharge part of the conveying device, so that the powder in the cooling furnace is An airtight chamber is provided that communicates the granule outlet with the inlet of the rotary valve and isolates the conveying device from the outside air, and the chute wall of the rotary valve supply port facing the rotor rotation direction is joined to the outer circumference of the rotary valve casing. The part is formed so that it is located far from the falling locus of the powder and granular material,
Discharge of a vertical cooling furnace for powder and granular materials, characterized in that the rotary valve discharge port opens from near horizontally, and the conveying device is configured to be able to control a supply amount smaller than the powder and granule cutting capacity of the rotary valve. Device.
JP4632783A 1983-03-19 1983-03-19 Discharge device of vertical cooling furnace for particulate body Granted JPS59173128A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4632783A JPS59173128A (en) 1983-03-19 1983-03-19 Discharge device of vertical cooling furnace for particulate body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4632783A JPS59173128A (en) 1983-03-19 1983-03-19 Discharge device of vertical cooling furnace for particulate body

Publications (2)

Publication Number Publication Date
JPS59173128A JPS59173128A (en) 1984-10-01
JPS6248530B2 true JPS6248530B2 (en) 1987-10-14

Family

ID=12744049

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4632783A Granted JPS59173128A (en) 1983-03-19 1983-03-19 Discharge device of vertical cooling furnace for particulate body

Country Status (1)

Country Link
JP (1) JPS59173128A (en)

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