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JPH01119633A - Raw material and fuel supplying device - Google Patents

Raw material and fuel supplying device

Info

Publication number
JPH01119633A
JPH01119633A JP27329487A JP27329487A JPH01119633A JP H01119633 A JPH01119633 A JP H01119633A JP 27329487 A JP27329487 A JP 27329487A JP 27329487 A JP27329487 A JP 27329487A JP H01119633 A JPH01119633 A JP H01119633A
Authority
JP
Japan
Prior art keywords
raw material
fuel
tank
valve
raw materials
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
JP27329487A
Other languages
Japanese (ja)
Other versions
JP2505497B2 (en
Inventor
Nobumasa Iemori
伸正 家守
Yasuo Oshima
尾島 康夫
Yoshiaki Mori
芳秋 森
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.)
Sumitomo Metal Mining Co Ltd
Original Assignee
Sumitomo Metal Mining 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 Sumitomo Metal Mining Co Ltd filed Critical Sumitomo Metal Mining Co Ltd
Priority to JP27329487A priority Critical patent/JP2505497B2/en
Publication of JPH01119633A publication Critical patent/JPH01119633A/en
Application granted granted Critical
Publication of JP2505497B2 publication Critical patent/JP2505497B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Manufacture And Refinement Of Metals (AREA)

Abstract

PURPOSE:To enable the rapid change of the kinds of raw materials and the ratio of the raw materials and fuel in compliance with the change in the condition in a flash smelting furnace by feeding the raw materials and fuel separately, joining the materials and fuel just before a lance pipe to supply both to the lance pipe and providing a raw material storage tank to the part right above a raw material supplying tank. CONSTITUTION:A feeding device 35a of the raw material storage tank is stopped at the time of changing the raw materials according to the furnace condition, for example, changing the raw materials E to F. After the raw materials E in a raw material supplying tank 39 are fed to a raw material pressurizing tank 41, the feeder 35b of the raw material storage tank in the lower part of the raw material storage tank is operated to store the raw materials F in the raw material supplying tank 39. A raw material supplying valve 40 is opened to supply the raw materials E in the tank 39 to the pressurizing tank 41 when the raw materials E in the tank 41 are substantially run out. The fuel feeding rate and the flow rate of the gas for reaction are controlled by changing the set value of a feeding device 31 of the fuel pressurizing tank and the set value of a control valve 56.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は自熔製錬炉のセトラー部に原料と燃料を装入す
るランスパイプへの、これら原料と燃料の供給装置の改
善に関するものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to an improvement in a device for supplying raw materials and fuel to a lance pipe for charging raw materials and fuel into the settler section of a flash smelting furnace. be.

[従来の技術] ランスパイプを用いる自熔製錬炉においては、ランスパ
イプより鉱石、溶剤、煙灰等の製錬原料(以下単に原料
と記す。)と微粉炭等の固体燃料(以下単に燃料と記す
。)とを反応用気体と共に炉内セトラー部の熔体中に吹
き込むことにより、鉱石の溶解能力の大幅増加を可能と
するが、このための設備として、従来より第2図に示す
ような装置が用いられている。
[Prior Art] In a flash smelting furnace using a lance pipe, smelting raw materials such as ore, solvent, and smoke ash (hereinafter simply referred to as raw materials) and solid fuel such as pulverized coal (hereinafter simply referred to as fuel) are ) can be injected into the melt in the settler section of the furnace together with a reaction gas, making it possible to significantly increase the ability to dissolve ore. equipment is used.

第2図において、Aは給鉱を貯蔵する貯蔵槽である。1
は切出し装置であり、ベルトコンベア2の一端に接続さ
れ、ベルトコンベア2の他端はパケットコンベア3の受
入れ口に接続されている。
In FIG. 2, A is a storage tank for storing feed ore. 1
is a cutting device, which is connected to one end of the belt conveyor 2, and the other end of the belt conveyor 2 is connected to the receiving port of the packet conveyor 3.

パケットコンベア3の排出端はチェンコンベア4の一端
に接続され、チェンコンベア4の他端は供給タンク受入
弁5の上部に開口している。供給タンク受入弁5の下に
は供給タンク6が設けられ、供給タンク6の下部には供
給弁7を介し、リフトタンク8が設けられている。
A discharge end of the packet conveyor 3 is connected to one end of a chain conveyor 4, and the other end of the chain conveyor 4 is open to the upper part of the supply tank receiving valve 5. A supply tank 6 is provided below the supply tank receiving valve 5, and a lift tank 8 is provided below the supply tank 6 via a supply valve 7.

搬送気体用配管9は減圧弁11、加圧弁12゜13を介
しリフトタンク下部に接続している。また、搬送気体用
配管10は減圧弁16、ブースター弁17を介し、合流
点P1でリフトタンク8に設けられた給鉱供給管14と
合流している。
The carrier gas pipe 9 is connected to the lower part of the lift tank via a pressure reducing valve 11 and pressurizing valves 12 and 13. Further, the carrier gas pipe 10 merges with the ore supply pipe 14 provided in the lift tank 8 at a confluence point P1 via a pressure reducing valve 16 and a booster valve 17.

次に第2図の装置の作用を説明する。Next, the operation of the apparatus shown in FIG. 2 will be explained.

貯蔵槽Aには前もって原料と燃料とを混合して得たラン
スパイプへの吹込物、すなわち給鉱を貯蔵する。
Storage tank A stores the material to be injected into the lance pipe, that is, the feed ore obtained by mixing raw materials and fuel in advance.

吹錬中、搬送気体用配管9を通った圧縮空気等の搬送用
気体Bは、減圧弁11、加圧弁12.13を通りリフト
タンク8内に導かれる。一方、搬送気体用配管10を通
った搬送用気体Bは減圧弁16、ブースター弁17を通
りリフトタンク8からの給鉱供給弁管14との合流点P
1に導かれる。
During blowing, the carrier gas B such as compressed air that has passed through the carrier gas pipe 9 is guided into the lift tank 8 through the pressure reducing valve 11 and the pressurizing valves 12 and 13. On the other hand, the transport gas B that has passed through the transport gas pipe 10 passes through the pressure reducing valve 16 and the booster valve 17 and reaches the confluence point P with the ore supply valve pipe 14 from the lift tank 8.
I am guided by 1.

これらの搬送用気体Bによってリフトタンク8内の給鉱
は給鉱供給管14、給鉱供給弁15を通りランスパイプ
18へ圧送され、流量調節弁20にて圧力を調節された
反応用気体Cと共にランスパイプ18より炉内19に吹
込まれる。
The feed ore in the lift tank 8 is fed under pressure to the lance pipe 18 through the ore supply pipe 14 and the ore supply valve 15 by these transport gases B, and the reaction gas C whose pressure is regulated by the flow rate control valve 20 At the same time, it is blown into the furnace 19 from the lance pipe 18.

リフトタンク8内の給鉱が所定量以下になると、均圧配
管22に設けられた均圧弁23を開放し、供給タンク6
内の圧力とリフトタンク8内の圧力を同じにした後、供
給弁7を開け、供給タンク6内の給鉱をリフトタンク8
に供給する。
When the supply ore in the lift tank 8 falls below a predetermined amount, the pressure equalization valve 23 provided in the pressure equalization pipe 22 is opened, and the supply tank 6
After making the pressure in the tank and the pressure in the lift tank 8 the same, the supply valve 7 is opened and the feed ore in the supply tank 6 is transferred to the lift tank 8.
supply to.

供給タンク6内の給鉱が全量落下したのを確認した後、
供給弁7、均圧弁23を閉じ、供給タンクに設けた圧抜
き弁24を開放し、供給タンク6内の圧力を大気圧まで
低下させる。
After confirming that all the feed ore in the supply tank 6 has fallen,
The supply valve 7 and the pressure equalization valve 23 are closed, and the pressure relief valve 24 provided in the supply tank is opened to reduce the pressure inside the supply tank 6 to atmospheric pressure.

その後、供給タンク受入弁5を、開放し、チェンコンベ
ア4、パケットコンベア3、ベルトコンベア2、切出し
装置1を順次運転し供給タンク6に給鉱を貯蔵する。所
定量の給鉱が供給タンク6内に貯蔵された時、切出し装
M1、ベルトコンベア2、パケットコンベア3、チェン
コンベア4の順番に停止され、供給タンク受入弁5、圧
抜き弁24が閉じられる。以後、この一連の操作は供給
タンク6、リフトタンク8内の給鉱の量を検出すること
により連続的に行われる。
Thereafter, the supply tank receiving valve 5 is opened, and the chain conveyor 4, packet conveyor 3, belt conveyor 2, and cutting device 1 are sequentially operated to store the feed ore in the supply tank 6. When a predetermined amount of feed ore is stored in the supply tank 6, the cutter M1, belt conveyor 2, packet conveyor 3, and chain conveyor 4 are stopped in this order, and the supply tank receiving valve 5 and pressure release valve 24 are closed. . Thereafter, this series of operations is continuously performed by detecting the amount of ore to be fed in the supply tank 6 and lift tank 8.

ところで、給鉱中の原料と燃料の比は単位時間当たりの
炉への装入間、原料の組成、及び反応用気体中の酸素濃
度等により熱収支を計算し決定されるが、上記従来の給
鉱供給装置では事前に大量の給鉱を作成し貯蔵している
ため、炉内の状況の変化に応じ原料組成を変更しようと
する時や給鉱量を変化させる時には、迅速な対応が取り
にくいという問題点がある。
By the way, the ratio of raw material to fuel during ore feeding is determined by calculating the heat balance based on the charging time to the furnace per unit time, the composition of the raw material, the oxygen concentration in the reaction gas, etc. Since the feed supply equipment creates and stores a large amount of feed ore in advance, it is possible to quickly respond when changing the raw material composition or the amount of ore feed in response to changes in the situation inside the furnace. The problem is that it is difficult.

[発明が解決しようとする問題点] 本発明はランスパイプを用いる自熔製錬炉において、ラ
ンスパイプに原料及び燃料を供給するに際し、供給する
原料の種類や原料と燃料との比、あるいは給鉱量を変化
させる際に迅速に対応できるようにする装置に関するも
のである。
[Problems to be Solved by the Invention] The present invention provides for a flash smelting furnace using a lance pipe, in which raw materials and fuel are supplied to the lance pipe. This invention relates to a device that allows quick response when changing ore reserves.

[問題点を解決するための手段] この発明の装置は上記問題点を解決するために原料と燃
料とを別々に流送し、ランスパイプ手前で原料と燃料を
合一し、ランスパイプに供給すると共に原料供給タンク
の直上部に複数の原料貯蔵槽を設けることにより、自熔
製錬炉の炉内の状況変化に合わせ原料の種類や、原料と
燃料の比を迅速に変更できるようにしたものである。以
下この発明の実施例を第1図に基づいて説明する。
[Means for Solving the Problems] In order to solve the above-mentioned problems, the device of the present invention transports raw materials and fuel separately, combines the raw materials and fuel in front of the lance pipe, and supplies the raw materials and fuel to the lance pipe. At the same time, by installing multiple raw material storage tanks directly above the raw material supply tank, we have made it possible to quickly change the type of raw material and the ratio of raw materials to fuel according to changes in the internal conditions of the flash smelting smelting furnace. It is something. Embodiments of the present invention will be described below with reference to FIG.

Dは燃料貯蔵槽であり、E、Fは原料E1原料Fを貯蔵
する原料貯蔵槽である。
D is a fuel storage tank, and E and F are raw material storage tanks that store raw material E1 and raw material F.

燃料貯蔵槽切出し装置25はスクリューコンベア26の
一端に取り付けられ、スクリューコンベア26の他端は
燃料供給タンク27の上部に取り付けられた燃料供給タ
ンク受入弁28の上で開口している。
The fuel storage tank cutting device 25 is attached to one end of a screw conveyor 26, and the other end of the screw conveyor 26 opens above a fuel supply tank receiving valve 28 attached to the upper part of the fuel supply tank 27.

燃料供給タンク27の下には燃料供給弁29を介し燃料
加圧タンク30が設けられている。燃料加圧タンク30
の下部には燃料加圧タンク切出し装置31、スクリュー
コンベア32が設けられており、燃料流送管33に燃料
を送り込むことができるようになっている。また、燃料
加圧タンク30には燃料の切り出しを支障なく行なうた
めの加圧配管58が設けられている。そして、燃料流送
管33はP2で原料流送管34と合流している。
A fuel pressurized tank 30 is provided below the fuel supply tank 27 via a fuel supply valve 29 . Fuel pressurized tank 30
A fuel pressurized tank cut-out device 31 and a screw conveyor 32 are provided at the bottom of the fuel tank, so that fuel can be fed into a fuel flow pipe 33. Further, the fuel pressurization tank 30 is provided with a pressurization pipe 58 for removing the fuel without any trouble. The fuel flow pipe 33 joins the raw material flow pipe 34 at P2.

また、原料貯蔵槽Eの下部に設けられた原料貯蔵槽切出
し装@35aはスクリューコンベア36の一端に取り付
けられ、スクリューコンベア36の他端は原料供給タン
ク39の上部に取り付けられた原料供給タンク受入弁3
8の上で開口している。
In addition, the raw material storage tank cutout device @35a provided at the lower part of the raw material storage tank E is attached to one end of the screw conveyor 36, and the other end of the screw conveyor 36 is connected to the raw material supply tank receiving unit attached to the upper part of the raw material supply tank 39. Valve 3
It opens above 8.

また、原料貯蔵槽Fの下部に設けられた原料貯蔵槽切出
し装置35bはシュート37を介し原料供給タンク39
の上部に取り付けられた原料供給タンク受入弁38の上
で開口している。
Further, the raw material storage tank cutting device 35b provided at the lower part of the raw material storage tank F is connected to the raw material supply tank 39 through the chute 37.
It opens above a raw material supply tank receiving valve 38 attached to the top of the tank.

原料供給タンク39の下には原料供給弁40を介し原料
加圧タンク41が設けられている。原料加圧タンク41
の下部には原料加圧タンク切出し装置42、スクリュー
コンベア43が設けられており、原料流送管34に原料
を送り込むことができるようになっている。また、原料
加圧タンク41には原料の切出しを支障なく行なうため
の加圧配管44が設けらている。そして、原料流送管3
4はP2で燃料流送管33と合流した後、ランスホース
45を介してランスパイプ18と接続している。
A raw material pressurized tank 41 is provided below the raw material supply tank 39 via a raw material supply valve 40 . Raw material pressurized tank 41
A raw material pressurized tank cut-out device 42 and a screw conveyor 43 are provided at the bottom of the raw material pressurized tank and a screw conveyor 43 are provided so that the raw material can be fed into the raw material flow pipe 34. Further, the raw material pressurizing tank 41 is provided with a pressurizing pipe 44 for cutting out the raw material without any trouble. And raw material flow pipe 3
4 joins the fuel flow pipe 33 at P2, and then connects to the lance pipe 18 via a lance hose 45.

[作 用コ 次に上記実施例について作用態様を説明する。[Production use] Next, the mode of operation of the above embodiment will be explained.

吹錬中、燃料は燃料加圧タンク30より燃料加圧タンク
切出し装置31により調節されながら切出され、スクリ
ューコンベア32を介し燃料流送管33に供給される。
During blowing, fuel is cut out from the fuel pressurized tank 30 while being regulated by a fuel pressurized tank cut-out device 31, and is supplied to a fuel flow pipe 33 via a screw conveyor 32.

供給される燃料量は、単位時間当たりの装入量、原料の
組成、及び反応用気体中の酸素濃度等により熱収支を計
算し決定される。
The amount of fuel to be supplied is determined by calculating the heat balance based on the amount charged per unit time, the composition of the raw materials, the oxygen concentration in the reaction gas, etc.

搬送用気体Bは減圧弁46を通り、一部は分岐した後、
加圧配t!!58を通り、途中に設けられた加圧弁47
により調節された後、燃料加圧タンク30に入り燃料加
圧タンク30の内圧を搬送圧力より若干高目にし、切出
しを良好にする。
The conveying gas B passes through the pressure reducing valve 46, and after part of it branches off,
Pressurized! ! 58 and a pressurizing valve 47 provided on the way.
After being adjusted, the fuel enters the pressurized fuel tank 30 and the internal pressure of the pressurized fuel tank 30 is made slightly higher than the conveying pressure to improve cutting.

他方は加圧弁48.49を通り、スクリューコンベア3
2より供給された燃料を合流点P2まで搬送する。
The other side passes through the pressurizing valves 48 and 49 and is connected to the screw conveyor 3.
The fuel supplied from P2 is transported to the confluence P2.

燃料加圧タンク30内の燃料が所定量以下になると、燃
料供給弁29が開かれ、燃料が燃料加圧タンク30内に
供給される。燃料供給タンク27が空になったのが確認
された後、燃料供給弁29は閉じられ、圧抜き弁50が
開かれ燃料供給タンク27内の圧力を大気圧まで低下さ
せる。燃料供給タンク27内の圧力が低下したのが確認
された後、燃料供給タンク受入弁28が開かれ、次いで
スクリューコンベア26、燃料貯蔵槽切出し装置25が
運転され燃料供給タンク27内に燃料が供給される。
When the fuel in the pressurized fuel tank 30 becomes less than a predetermined amount, the fuel supply valve 29 is opened and fuel is supplied into the pressurized fuel tank 30. After confirming that the fuel supply tank 27 is empty, the fuel supply valve 29 is closed and the pressure relief valve 50 is opened to reduce the pressure inside the fuel supply tank 27 to atmospheric pressure. After it is confirmed that the pressure inside the fuel supply tank 27 has decreased, the fuel supply tank receiving valve 28 is opened, and then the screw conveyor 26 and the fuel storage tank cut-out device 25 are operated to supply fuel into the fuel supply tank 27. be done.

所定量の燃料が燃料供給タンク27内に貯蔵された侵、
燃料貯蔵槽切出し装置25、スクリューコンベア26の
順に停止され、その後燃料供給タンク受入弁28と圧抜
き弁50が閉じられる。
When a predetermined amount of fuel is stored in the fuel supply tank 27,
The fuel storage tank extraction device 25 and the screw conveyor 26 are stopped in this order, and then the fuel supply tank receiving valve 28 and the pressure release valve 50 are closed.

以後、この一連の操作は供給タンク内、加圧タンク内の
燃料の量を検出することにより自動的に行われる。
Thereafter, this series of operations is automatically performed by detecting the amount of fuel in the supply tank and the pressurized tank.

一方、原料は原料加圧タンク41より原料加圧タンク切
出し装置42により調節されながら切出され、スクリュ
ーコンベア43を介し原料流送管34に供給される。
On the other hand, the raw material is cut out from the raw material pressurized tank 41 while being regulated by the raw material pressurized tank cutting device 42, and is supplied to the raw material flow pipe 34 via the screw conveyor 43.

搬送用気体Bは減圧弁51を通り、一部は分岐した後、
加圧配管44を通り、途中に設けられた加圧弁52によ
り調節された後、原料加圧タンク41に入り原料加圧タ
ンク41の内圧を搬送圧力より若干高目にし、切出しを
良好にする。他方は加圧弁53.54を通り、スクリュ
ーコンベア43より供給された原料を合流点P2まで搬
送する。
The transport gas B passes through the pressure reducing valve 51, and after part of it branches off,
After passing through the pressurizing pipe 44 and being regulated by a pressurizing valve 52 provided midway, the material enters the raw material pressurizing tank 41 and the internal pressure of the raw material pressurizing tank 41 is made slightly higher than the conveying pressure to improve cutting. The other one passes through pressurizing valves 53 and 54 and conveys the raw material supplied from the screw conveyor 43 to the confluence point P2.

P2で合流した原料および燃料はランスホース45を介
しランスパイプ18に供給され、反応用気体配管21、
ランスホース55を経てランスパイプ18に供給された
反応用気体Cと共に自熔製錬炉の炉内19に吹き込まれ
る。
The raw materials and fuel combined at P2 are supplied to the lance pipe 18 via the lance hose 45, and the reaction gas pipe 21,
It is blown into the furnace interior 19 of the flash smelting furnace together with the reaction gas C supplied to the lance pipe 18 via the lance hose 55.

なお、反応用気体の流mi節は調節弁56の開度により
行われる。
Note that the flow rate mi of the reaction gas is determined by the opening degree of the control valve 56.

原料加圧タンク41の原料が所定量以下になると、自動
的に原料供給弁40が開き、原料供給タンク39内の原
料が原料加圧タンク41内に供給される。原料供給タン
ク39内が空になったのが確認された後、原料供給弁4
0が閉じられ、原料供給タンク39の圧抜き弁57が開
放され、各供給タンク内の圧を大気圧と同じにする。次
いで、原料供給タンク受入弁38が開き、スクリューコ
ンベア36、原料貯蔵槽切出し装置135aが運転され
原料Eが、あるいは、原料貯蔵槽切出し装置35bが運
転されシュート37を介し原料Fが、あるいはスクリュ
ーコンベア36、原料貯蔵槽切出し装置35a 、35
bが運転され、原料Eと原料Fとが所定の割合で原料供
給タンク39に貯蔵される。
When the raw material in the raw material pressurized tank 41 becomes less than a predetermined amount, the raw material supply valve 40 is automatically opened, and the raw material in the raw material supply tank 39 is supplied into the raw material pressurized tank 41. After confirming that the raw material supply tank 39 is empty, the raw material supply valve 4
0 is closed, and the pressure relief valves 57 of the raw material supply tanks 39 are opened to make the pressure in each supply tank the same as atmospheric pressure. Next, the raw material supply tank receiving valve 38 is opened, and the screw conveyor 36 and the raw material storage tank cut-out device 135a are operated to transfer the raw material E, or the raw material storage tank cut-out device 35b is operated to transfer the raw material F through the chute 37, or the screw conveyor 36, raw material storage tank cutting device 35a, 35
b is operated, and raw material E and raw material F are stored in the raw material supply tank 39 at a predetermined ratio.

所定量の原料が原料供給タンク39に貯蔵された後スク
リューコンベア36、原料貯蔵槽切出し装置35a、あ
るいは35bあるいはその双方が停止され原料供給タン
ク受入弁38、圧抜き弁57が閉じられる。
After a predetermined amount of raw material is stored in the raw material supply tank 39, the screw conveyor 36, the raw material storage tank cutting device 35a or 35b, or both are stopped, and the raw material supply tank receiving valve 38 and the pressure release valve 57 are closed.

これ以後この一連の操作は原料供給タンク、原料加圧タ
ンク内の原料の量を検出することにより自動的に行われ
る。
After this, this series of operations is automatically performed by detecting the amount of raw material in the raw material supply tank and the raw material pressurizing tank.

炉況に応じ原料を変更する時、例えば原料EからFへ変
更する時には、原料貯蔵槽切出し装置35aを停止し、
次いでスクリューコンベア36を停止し、原料供給タン
ク39内の原料Eが原料加圧タンク41に払い出された
後、原料貯蔵槽F下部の原料貯蔵槽切出し装置35bを
作動させ、原料Fを原料供給タンク39に貯蔵する。
When changing the raw material according to the furnace condition, for example, when changing from raw material E to F, the raw material storage tank cutting device 35a is stopped,
Next, the screw conveyor 36 is stopped, and after the raw material E in the raw material supply tank 39 is delivered to the raw material pressure tank 41, the raw material storage tank cutting device 35b at the lower part of the raw material storage tank F is activated, and the raw material F is supplied as a raw material. It is stored in tank 39.

そして、原料加圧タンク41内の原料Eがほとんどなく
なったときに原料供給弁40を開き、原料供給タンク3
9内の原料Fを原料加圧タンク41に供給する。次いで
燃料加圧タンク切出し装@31の設定値と調節弁56の
設定値を変更し、燃料の切出し量と反応用気体の流通を
調節する。
Then, when the raw material E in the raw material pressurized tank 41 is almost exhausted, the raw material supply valve 40 is opened, and the raw material supply tank 3
The raw material F in 9 is supplied to the raw material pressurized tank 41. Next, the set values of the fuel pressurized tank cut-out device @31 and the set values of the control valve 56 are changed to adjust the cut-out amount of fuel and the flow of reaction gas.

また、原料E、原料Fを混合して吹錬を行なっている場
合にその原料比を変更しようとする時には、原料貯蔵槽
切出し装置35a、35bの設定値を調節し、夫々の切
出し量を変更する。この変更に伴う燃料量の変更は上記
と同様原料加圧タンク41より混合比変更模の原料が切
出されるとほぼ同時に燃料加圧タンク切出し装置31の
設定値と調節弁56の設定を変更し、燃料の切出し量と
反応用気体の流量を調節する。
Furthermore, when blowing is performed by mixing raw material E and raw material F, when attempting to change the raw material ratio, the set values of the raw material storage tank cutting devices 35a and 35b are adjusted to change the respective cutting amounts. do. The change in fuel amount associated with this change is similar to the above, and the setting value of the fuel pressurization tank cutting device 31 and the setting of the control valve 56 are changed almost at the same time as the raw material whose mixture ratio has been changed is cut out from the raw material pressurization tank 41. , adjust the amount of fuel cut out and the flow rate of reaction gas.

また、炉況により燃料のみ吹き込む必要が生じた時は、
原料加圧タンク切出し装置42とスクリューコンベア4
3を停止し調節弁56を調節し、反応用気体の流量を調
節する。
Also, when it becomes necessary to inject only fuel due to furnace conditions,
Raw material pressurized tank cutting device 42 and screw conveyor 4
3 and adjust the control valve 56 to adjust the flow rate of the reaction gas.

なお、本実施例では燃料貯蔵槽や原料貯蔵槽とそれぞれ
の供給タンクとの間の燃料や原料の搬送装置としてスク
リューコンベアあるいは自由落下を利用したシュートを
用いているが、この搬送装置は目的さえ達成できれば種
類は問わないことは言うまでもない。
In this example, a screw conveyor or a chute that utilizes free fall is used as a conveyance device for fuel and raw materials between the fuel storage tank or raw material storage tank and each supply tank, but this conveyance device does not meet the purpose. It goes without saying that the type does not matter as long as it can be achieved.

また、本実施例では説明を簡略にするため原料供給タン
クの直上に2個の原料貯蔵槽を持つ例を示したが、必要
に応じ3個以上の原料貯蔵槽を持たせることができる。
Further, in this embodiment, in order to simplify the explanation, an example is shown in which two raw material storage tanks are provided directly above the raw material supply tank, but three or more raw material storage tanks can be provided as necessary.

[発明の効果] 以上述べたように、本発明の装置は原料供給タンクの直
上に複数個の原料貯蔵槽を持っているため、原料の種類
の変更、あるいは混合比の変更が簡単にでき、且つ原料
と燃料との搬送系統が分かれていることにより、原料の
変更、あるいは混合比の変更に伴9て必要とされる燃F
l量の変更を簡単に行なうことができるので、常に炉況
に応じた最適の吹き込み調合を維持することができる。
[Effects of the Invention] As described above, since the apparatus of the present invention has a plurality of raw material storage tanks directly above the raw material supply tank, it is possible to easily change the type of raw materials or change the mixing ratio. In addition, because the transportation systems for raw materials and fuel are separated, the fuel F required when changing raw materials or changing the mixing ratio is reduced.
Since the amount of 1 can be easily changed, the optimum blowing mixture according to the furnace conditions can be maintained at all times.

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

第1図は本発明の実施例を示す図であり、第2図は従来
の装置を示す図である。 1・・・切出し装置、2・・・ベルトコンベア、3・・
・パケットコンベア、4・・・チェンコンベア、5・・
・供給タンク受入弁、6・・・供給タンク、7・・・供
給弁、8・・・リフトタンク、9・・・搬送気体用配管
、10・・・搬送気体用配管、11・・・減圧弁、12
・・・加圧弁、13・・・加圧弁、14・・・給鉱供給
管、15・・・給鉱供給弁、16・・・減圧弁、17・
・・ブースター弁、18・・・ランスパイプ、19・・
・炉内、20・・・流通調節弁、21・・・反応用気体
配管、22・・・均圧配管、23・・・均圧弁、24・
・・圧扱き弁、25・・・燃料貯蔵槽切出し装置、26
・・・スクリューコンベア、27・・・燃料供給タンク
、28・・・燃料供給タンク受入弁、29・・・燃料供
給弁、30・・・燃料加圧タンク、31・・・燃料加圧
タンク切出し装置、32・・・スクリューコンベア、3
3・・・燃料流送管、34・・・原料流送管、35a・
・・原料貯蔵槽切出し装置、35b・・・原料貯蔵槽切
出し装置、36・・・スクリューコンベア、37・・・
シュート、38・・・原料供給タンク受入弁、39・・
・原料供給タンク、40・・・原料供給弁、41・・・
原料加圧タンク、42・・・原料加圧タンク切出し装置
、43・・・スクリューコンベア、44・・・加圧配管
、45・・・ランスホース、46・・・減圧弁、47・
・・加圧弁、48・・・加圧弁、49・・・加圧弁、5
0・・・圧抜き弁、51・・・減圧弁、52・・・加圧
弁、53・・・加圧弁、54・・・加圧弁、55・・・
ランスホース、56・・・調節弁、57・・・圧抜き弁
、58・・・加圧配管、A・・・貯蔵槽、B・・・搬送
用気体、C・・・反応用気体、D・・・燃料貯蔵槽、E
・・・原料貯蔵槽、F・・・原料貯蔵槽。 特許出願人 住友金属鉱山株式会社
FIG. 1 is a diagram showing an embodiment of the present invention, and FIG. 2 is a diagram showing a conventional device. 1... Cutting device, 2... Belt conveyor, 3...
・Packet conveyor, 4...Chain conveyor, 5...
・Supply tank reception valve, 6... Supply tank, 7... Supply valve, 8... Lift tank, 9... Piping for carrier gas, 10... Piping for carrier gas, 11... Depressurization valve, 12
... Pressure valve, 13 ... Pressure valve, 14 ... Ore feed supply pipe, 15 ... Ore feed supply valve, 16 ... Pressure reducing valve, 17.
...Booster valve, 18...Lance pipe, 19...
・Furnace interior, 20...Flow control valve, 21...Reaction gas piping, 22...Pressure equalization piping, 23...Pressure equalization valve, 24.
... Pressure handling valve, 25 ... Fuel storage tank cut-out device, 26
... Screw conveyor, 27 ... Fuel supply tank, 28 ... Fuel supply tank receiving valve, 29 ... Fuel supply valve, 30 ... Fuel pressurization tank, 31 ... Fuel pressurization tank cutout Device, 32...Screw conveyor, 3
3... Fuel flow pipe, 34... Raw material flow pipe, 35a.
... Raw material storage tank cutting device, 35b... Raw material storage tank cutting device, 36... Screw conveyor, 37...
Chute, 38... Raw material supply tank receiving valve, 39...
・Raw material supply tank, 40...Raw material supply valve, 41...
Raw material pressurized tank, 42... Raw material pressurized tank cutting device, 43... Screw conveyor, 44... Pressurized piping, 45... Lance hose, 46... Pressure reducing valve, 47...
... Pressure valve, 48 ... Pressure valve, 49 ... Pressure valve, 5
0... Pressure release valve, 51... Pressure reducing valve, 52... Pressurizing valve, 53... Pressurizing valve, 54... Pressurizing valve, 55...
Lance hose, 56...Control valve, 57...Pressure relief valve, 58...Pressure piping, A...Storage tank, B...Transportation gas, C...Reaction gas, D ...Fuel storage tank, E
...Raw material storage tank, F...Raw material storage tank. Patent applicant Sumitomo Metal Mining Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 自熔製錬炉のセトラー部に設けたランスパイプに原料と
燃料を供給する装置において、切出し手段と搬送手段と
を備えた複数の原料用貯蔵槽と、これら貯蔵相から切出
し搬送された一種あるいは複数種の原料粉をまとめて収
容する原料供給ホッパーと、該ホッパーの下部に弁を介
して接続された加圧ホッパーと、該加圧ホッパーより切
出された原料を気流状で輸送する原料流送管と、同様に
切出し手段と搬送手段とを備えた固体燃料粉貯蔵槽と、
該貯蔵槽から切出し、搬送された燃料粉を収容する燃料
供給ホッパーと、該ホッパーの下部に弁を介して接続さ
れた加圧ホッパーと、該加圧ホッパーから切出された燃
料を気流状で輸送する燃料流送管とを備え、前記原料流
送管と燃料流送管とがランスパイプの供給口より前方で
合流されていることを特徴とする原料と燃料の供給装置
In a device for supplying raw materials and fuel to a lance pipe provided in a settler section of a flash smelting furnace, there are a plurality of storage tanks for raw materials equipped with a cutting means and a conveying means, and a type or fuel that is cut and conveyed from these storage phases. A raw material supply hopper that collectively accommodates multiple types of raw material powder, a pressurized hopper connected to the lower part of the hopper via a valve, and a raw material flow that transports the raw material cut from the pressurized hopper in an air stream. a solid fuel powder storage tank comprising a conduit, a cutting means and a conveying means;
A fuel supply hopper that stores the fuel powder cut out from the storage tank and transported; a pressurized hopper connected to the lower part of the hopper via a valve; 1. A supply device for raw materials and fuel, comprising: a fuel flow pipe for transporting the raw material and the fuel, the raw material flow pipe and the fuel flow pipe being joined in front of a supply port of a lance pipe.
JP27329487A 1987-10-30 1987-10-30 Material and fuel supply equipment Expired - Fee Related JP2505497B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27329487A JP2505497B2 (en) 1987-10-30 1987-10-30 Material and fuel supply equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27329487A JP2505497B2 (en) 1987-10-30 1987-10-30 Material and fuel supply equipment

Publications (2)

Publication Number Publication Date
JPH01119633A true JPH01119633A (en) 1989-05-11
JP2505497B2 JP2505497B2 (en) 1996-06-12

Family

ID=17525848

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27329487A Expired - Fee Related JP2505497B2 (en) 1987-10-30 1987-10-30 Material and fuel supply equipment

Country Status (1)

Country Link
JP (1) JP2505497B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2373313A (en) * 2001-01-17 2002-09-18 Linston Ltd Materials introduced by lance into furnace
CN1325179C (en) * 2005-06-09 2007-07-11 上海交通大学 Method of electrodynamics for quick restoring soil polluted by heavy metal in situ

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2373313A (en) * 2001-01-17 2002-09-18 Linston Ltd Materials introduced by lance into furnace
CN1325179C (en) * 2005-06-09 2007-07-11 上海交通大学 Method of electrodynamics for quick restoring soil polluted by heavy metal in situ

Also Published As

Publication number Publication date
JP2505497B2 (en) 1996-06-12

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