JPH03100112A - Method for operating circulating fluidized reduction furnace of powdery ore and reduction furnace - Google Patents
Method for operating circulating fluidized reduction furnace of powdery ore and reduction furnaceInfo
- Publication number
- JPH03100112A JPH03100112A JP23963989A JP23963989A JPH03100112A JP H03100112 A JPH03100112 A JP H03100112A JP 23963989 A JP23963989 A JP 23963989A JP 23963989 A JP23963989 A JP 23963989A JP H03100112 A JPH03100112 A JP H03100112A
- Authority
- JP
- Japan
- Prior art keywords
- ore
- powdery
- reduction furnace
- downtake
- tube
- 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
Links
- 238000000034 method Methods 0.000 title claims description 7
- 239000002245 particle Substances 0.000 claims description 26
- 238000001514 detection method Methods 0.000 claims description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 14
- 229910052742 iron Inorganic materials 0.000 abstract description 7
- WWYNJERNGUHSAO-XUDSTZEESA-N (+)-Norgestrel Chemical compound O=C1CC[C@@H]2[C@H]3CC[C@](CC)([C@](CC4)(O)C#C)[C@@H]4[C@@H]3CCC2=C1 WWYNJERNGUHSAO-XUDSTZEESA-N 0.000 abstract 1
- 239000007790 solid phase Substances 0.000 abstract 1
- 239000000843 powder Substances 0.000 description 6
- 239000002994 raw material Substances 0.000 description 5
- 230000007423 decrease Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000003723 Smelting Methods 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000011017 operating method Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Landscapes
- Manufacture Of Iron (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、鉄鉱石等の粉鉱石を循環流動せしめて還元す
る還元炉の操業方法と還元炉に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a reduction furnace and a method for operating a reduction furnace for circulating and reducing fine ore such as iron ore.
近年、高炉による製鉄法が設備投資額が大きく、また、
良質の塊成鉱やコークスを必要とする原料選択上の制約
等の問題点を解消した溶融還元製鉄法が出現した。In recent years, the iron manufacturing method using blast furnaces requires large capital investment, and
A smelting reduction iron-making process has emerged that solves problems such as restrictions on raw material selection that require high-quality agglomerate ore and coke.
この溶融還元製鉄法において予備還元に用いられる流動
還元炉は、鉄鉱石、還元ガスを装入して流動層反応を行
う上昇管からなる反応塔と、反応塔からガスと共に排出
された鉱石を、気体一固体分離のためのサイクロンで捕
集し、反応塔の下部に再度装入する下降管とからなる構
造を有する。The fluidized reduction furnace used for preliminary reduction in this smelting reduction ironmaking method consists of a reaction tower consisting of a riser tube in which iron ore and reducing gas are charged and a fluidized bed reaction is carried out, and the ore discharged from the reaction tower together with gas is It has a structure consisting of a downcomer pipe that collects gas with a cyclone for solid separation and reinjects it into the lower part of the reaction tower.
かかる流動還元炉の操業において、粒子下降管内の粒子
レベルが減少すると、上昇管に吹き込んだガスが粒子下
降管側に流れ、サイクロンでの捕集効率を減少させ、上
昇管内の粒子の流動も不安定なものとなる。In the operation of such a fluidized bed reduction reactor, when the particle level in the particle downcomer decreases, the gas blown into the riser will flow to the particle downcomer, reducing the collection efficiency of the cyclone, and the flow of particles in the riser will also stop. It becomes stable.
したがって、循環流動層の操業を安定させるには、下降
管内の粒子レベルの大幅な変動を防止する必要がある。Therefore, to stabilize the operation of a circulating fluidized bed, it is necessary to prevent large fluctuations in particle levels in the downcomer.
このための対応手段が種々開示されている。Various means for dealing with this have been disclosed.
例えば、実開昭62−160295号公報には下降管の
途中に断面積の大きい粒子滞留部をつ(す、その循環を
円滑に行うために供給[料に近い粒度構成の成品を排出
することが開示され、また、特願昭63−69239号
出願明細書には下降管内の流動粉体の管理レベルの2点
に圧力計による検出装置を設け、これによって下降管内
のレベル低下に伴い、反応塔への原料供給量を増加させ
て対応する還元炉の操業法が開示されている。For example, Japanese Utility Model Application No. 62-160295 discloses that a particulate retention part with a large cross-sectional area is provided in the middle of the downcomer pipe, and in order to ensure smooth circulation, a product with a particle size composition similar to that of the feed material is discharged. In addition, in the specification of Japanese Patent Application No. 63-69239, detection devices using pressure gauges are installed at two points at the control level of the fluidized powder in the downcomer, and as a result, as the level in the downcomer decreases, the reaction is detected. A method of operating a reduction furnace that increases the amount of feedstock fed to the column is disclosed.
このような下降管内の鉱石粉末のレベル調整に際して、
反応の進行しない粒子下降管内の粒子の滞留量を増加さ
せてレベル変動を吸収することは、循環系に無駄な粒子
滞留域を増加させ、装置としての効率が低下するばかり
ではなく、滞留域での粒子温度の低下を生じ熱効率上好
ましくない。When adjusting the level of ore powder in the downcomer,
Absorbing level fluctuations by increasing the amount of particles stagnant in the particle downcomer where the reaction does not proceed increases the wasteful particle stagnation area in the circulation system, which not only reduces the efficiency of the device, but also increases the amount of particles in the stagnation area. This causes a drop in particle temperature, which is unfavorable in terms of thermal efficiency.
また、下降管内のレベル低下に伴い反応塔への原料供給
量を増加させて対応する操業法に右いては、急激な下降
管内のレベル変化には対応できないという欠点がある。In addition, an operating method that increases the amount of raw material supplied to the reaction tower as the level in the downcomer decreases has the disadvantage that it cannot respond to sudden changes in the level in the downcomer.
本発明において解決すべき課題は、下降管内の循環鉱石
の滞留が少なく、また、反応塔への原料供給に影響を与
えず、従って全体の操業条件に格別の影響を与えずに下
降管内の粉鉱レベルを一定に保持できる手段を見出すこ
とにある。The problem to be solved by the present invention is that the accumulation of circulating ore in the downcomer is small, and the powder in the downcomer can be removed without affecting the raw material supply to the reaction tower, and therefore without particularly affecting the overall operating conditions. The goal is to find a way to keep the ore level constant.
本発明は、下降管内の鉱石粒子表面レベルを検知し、同
検知レベルが一定レベル以下に低下したときに、同下降
管内に直接鉱石粉末を供給することによってその課題を
達成した。The present invention has achieved this objective by detecting the surface level of ore particles in the downcomer and supplying ore powder directly into the downcomer when the detected level falls below a certain level.
粒子下降管内の粒子表面レベルを検知するとともに、レ
ベル低下時に速やかに対応できる比較的大きい粉鉱石供
給能力をもつ供給機構より粉鉱石を一時的に供給するこ
とにより粒子表面レベルの回復を達成する。これによっ
て、粒子下降管へのガスの吹き抜けが防止でき、常に安
定した還元操業が可能になる。The particle surface level is recovered by detecting the particle surface level in the particle downcomer pipe and temporarily supplying fine ore from a supply mechanism having a relatively large fine ore supplying capacity that can quickly respond when the level decreases. This prevents gas from blowing into the particle downcomer pipe, making stable reduction operation possible at all times.
以下、第1図に示す実施例に基づいて本発明を説明する
。The present invention will be explained below based on the embodiment shown in FIG.
同図において、流動還元炉10は反応層を形成する上昇
管1と部分還元粒子を再度上昇管1に戻すルートを形成
する下降管2とからなる。In the figure, a fluidized-bed reduction furnace 10 includes a riser 1 that forms a reaction layer and a downcomer 2 that forms a route for returning the partially reduced particles to the riser 1 again.
同図を参照して、原料供給口3より供給された粉鉱石4
は上昇管1の下方から供給される還元ガス5により流動
層を形成して還元される。反応後の還元ガス5はサイク
ロン6に入り、ガスに同伴された粒子は下降管2を介し
て上昇管1に戻る。Referring to the same figure, powder ore 4 supplied from raw material supply port 3
is reduced by forming a fluidized bed by the reducing gas 5 supplied from below the riser 1. The reducing gas 5 after the reaction enters the cyclone 6, and the particles entrained in the gas return to the riser pipe 1 via the downcomer pipe 2.
その過程で一部は成品として下降管2の取り出しロア、
もしくは流動層下部の成品取り出し口8から回収される
。また、9は下降管2に直接粉鉱石を供給する供給機構
を示す。同供給機構9は下降管2に取付けられたレベル
計11と、同レベル計11からの信号を受けて開閉する
開閉機構12を有する粉鉱石ホッパ13とからなる。In the process, some of the products are the lower part of the downcomer pipe 2,
Alternatively, it is collected from the product outlet 8 at the bottom of the fluidized bed. Further, 9 indicates a supply mechanism that directly supplies fine ore to the downcomer pipe 2. The supply mechanism 9 includes a level meter 11 attached to the downcomer pipe 2, and a fine ore hopper 13 having an opening/closing mechanism 12 that opens and closes in response to a signal from the level meter 11.
前記レベル計11としては、例えば特願昭63−692
39号出願明細書に開示した2点レベル検出法を用いる
ことによって、より精密なレベル管理が可能になる。As the level meter 11, for example, Japanese Patent Application No. 63-692
By using the two-point level detection method disclosed in the No. 39 application, more precise level control becomes possible.
この供給機構9は、レベル計11により下降管内の粒子
表面レベルが管理下限レベル以下になったとき、粉鉱石
ホッパ13の開閉機構12を開放して鉱石を下降管2内
に供給する。This supply mechanism 9 opens the opening/closing mechanism 12 of the fine ore hopper 13 to supply ore into the downcomer pipe 2 when the particle surface level in the downcomer pipe becomes below the control lower limit level as determined by the level meter 11 .
そして、下降管2内の鉱石レベルが管理レベルを超えた
とき、開閉機構12は閉じられ粉鉱石の供給は停止する
。When the ore level in the downcomer pipe 2 exceeds the control level, the opening/closing mechanism 12 is closed and the supply of fine ore is stopped.
これによって、下降管2内の鉱石レベル低下に迅速に対
応でき、レベル変動を最小にして循環流動還元炉の操業
を安定したものとすることができる。As a result, it is possible to quickly respond to a drop in the ore level in the downcomer pipe 2, minimize level fluctuations, and stabilize the operation of the circulating fluidized reduction furnace.
本発明によって以下の効果を奏することができる。 The following effects can be achieved by the present invention.
(1)粒子下降管容量を小さくしたまま下降管内の粒子
表面レベル変動と吹き抜けを防止することができるので
、循環流動還元炉の基本構造を回答変更することなく安
定操業が可能となる。(1) Since it is possible to prevent particle surface level fluctuations and blow-through in the downcomer pipe while keeping the particle downcomer capacity small, stable operation is possible without changing the basic structure of the circulating fluid reduction reactor.
(2)粒子下降管での滞留時間を減少できるので、粒子
温度の低下を低減でき、全体装置の稼動効率を上げるこ
とができ熱効率を向上できる。(2) Since the residence time of particles in the downcomer tube can be reduced, the drop in particle temperature can be reduced, and the operating efficiency of the entire apparatus can be increased, thereby improving thermal efficiency.
(3)安定操業が維持され、円滑に還元が進行し生産性
が向上する。(3) Stable operation is maintained, reduction progresses smoothly, and productivity improves.
第1図は本発明の実施例を示す図である。 1:上昇管 2:下降管 3:原料供給口 4:粉鉱石 5:還元ガス 6:サイクロン 7.8:成品取り出し口 9:粉鉱石供給機構 FIG. 1 is a diagram showing an embodiment of the present invention. 1: Ascending pipe 2: Descending pipe 3: Raw material supply port 4: Powder ore 5: Reducing gas 6: Cyclone 7.8: Product outlet 9: Fine ore supply mechanism
Claims (1)
ベルが一定レベル以下に低下した時に、同下降管内に外
系より直接粉鉱石を供給して下降管内の鉱石粒子表面レ
ベルを調整する粉鉱石の循環流動還元炉の操業方法。 2、下降管内の鉱石粒子表面レベルを検知する検知機構
と、同検知機構からの信号によって粉鉱石を下降管内に
供給する供給機構を設けた粉鉱石の循環流動還元炉。[Claims] 1. The surface level of ore particles in the downcomer is detected, and when the detected level drops below a certain level, fine ore is directly supplied into the downcomer from an external system to reduce the ore particles in the downcomer. A method of operating a circulating fluidized-bed reduction furnace for fine ore to adjust the surface level. 2. A circulating fluidized ore reduction furnace for fine ore, which is provided with a detection mechanism that detects the surface level of ore particles in the downcomer, and a supply mechanism that supplies fine ore into the downcomer based on a signal from the detection mechanism.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1239639A JPH0730378B2 (en) | 1989-09-14 | 1989-09-14 | Circulating fluidized-ore reduction furnace operation method and reduction furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1239639A JPH0730378B2 (en) | 1989-09-14 | 1989-09-14 | Circulating fluidized-ore reduction furnace operation method and reduction furnace |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03100112A true JPH03100112A (en) | 1991-04-25 |
JPH0730378B2 JPH0730378B2 (en) | 1995-04-05 |
Family
ID=17047706
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1239639A Expired - Fee Related JPH0730378B2 (en) | 1989-09-14 | 1989-09-14 | Circulating fluidized-ore reduction furnace operation method and reduction furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0730378B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109225592A (en) * | 2018-10-29 | 2019-01-18 | 中冶北方(大连)工程技术有限公司 | A kind of underground is crushed drop shaft level-sensing device and fixes and lifting device |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS51132500A (en) * | 1975-05-13 | 1976-11-17 | Fuji Photo Film Co Ltd | High dielectric composed substance |
JPH0330290A (en) * | 1989-06-27 | 1991-02-08 | Mitsubishi Cable Ind Ltd | Electroluminescence lamp |
-
1989
- 1989-09-14 JP JP1239639A patent/JPH0730378B2/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS51132500A (en) * | 1975-05-13 | 1976-11-17 | Fuji Photo Film Co Ltd | High dielectric composed substance |
JPH0330290A (en) * | 1989-06-27 | 1991-02-08 | Mitsubishi Cable Ind Ltd | Electroluminescence lamp |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109225592A (en) * | 2018-10-29 | 2019-01-18 | 中冶北方(大连)工程技术有限公司 | A kind of underground is crushed drop shaft level-sensing device and fixes and lifting device |
CN109225592B (en) * | 2018-10-29 | 2023-10-27 | 中冶北方(大连)工程技术有限公司 | Underground broken drop shaft charge level indicator is fixed and hoisting device |
Also Published As
Publication number | Publication date |
---|---|
JPH0730378B2 (en) | 1995-04-05 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP0534243B1 (en) | A method for treating gases and particulate solids in a fluid bed | |
RU2158769C2 (en) | Three-stage gear for reduction of fine-grain iron ore in fluidized layer | |
RU2128713C1 (en) | Device of three-stage furnace type with fluidized bed for reduction of finely-divided iron ore (versions) | |
CA2255811C (en) | Process for the treatment of particulate matter by fluidisation, and vessel with apparatus to carry out the treatment | |
US6224649B1 (en) | Method and apparatus for reducing iron-oxides-particles having a broad range of sizes | |
JPH03100112A (en) | Method for operating circulating fluidized reduction furnace of powdery ore and reduction furnace | |
AU704146B2 (en) | 2-stage fluidized bed furnace for pre-reducing fine iron ore and method for pre-reducing fine iron ore using the furnace | |
US6235079B1 (en) | Two step twin-single fluidized bed pre-reduction apparatus for pre-reducing fine iron ore, and method therefor | |
US6132489A (en) | Method and apparatus for reducing iron-oxides-particles having a broad range of sizes | |
AU728390B2 (en) | Method for treating particulate material in the fluidized bed method and vessel and plant for carrying out the method | |
AU1513200A (en) | Fluidized bed type fine iron ore reducing apparatus, and method therefor | |
JP2501662B2 (en) | Control method of ore retention in circulating fluidized bed preliminary reduction furnace | |
JP2981015B2 (en) | Operating method of circulating fluidized bed reactor | |
JPH03215621A (en) | Circulating fluidized bed prereduction for powdery iron ore | |
JPH0372012A (en) | Circulating fluidized bed pre-reduction furnace | |
JPH07268429A (en) | Operating method of fluidized bed prereduction device | |
JP2659589B2 (en) | Circulating fluidized bed reduction device | |
JPH03100113A (en) | Operating method of circulating fluidized bed for reducing powdery ore | |
JPH0637653B2 (en) | Operation method of fluidized-ore reduction furnace for fine ore | |
JPH01247515A (en) | Method for pre-reducing fine ore and out-of-furnace circulating type fluidized bed reduction furnace | |
JPH03177511A (en) | Method for operating fluidized bed pre-reduction furnace and fluidized bed pre-reduction furnace | |
JPH01247519A (en) | Outside circulating type fluidized bed furnace | |
JPH0754029A (en) | Method for pre-reducing grain circulating fluidized bed and apparatus therefor | |
JPH046778B2 (en) | ||
JPH01247988A (en) | External circulation type fluidized-bed furnace |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20080405 Year of fee payment: 13 |
|
FPAY | Renewal fee payment (event date is renewal date of database) |
Free format text: PAYMENT UNTIL: 20090405 Year of fee payment: 14 |
|
LAPS | Cancellation because of no payment of annual fees |