JPS5952681B2 - Floating layer level detection method in floating steelmaking process - Google Patents
Floating layer level detection method in floating steelmaking processInfo
- Publication number
- JPS5952681B2 JPS5952681B2 JP12592378A JP12592378A JPS5952681B2 JP S5952681 B2 JPS5952681 B2 JP S5952681B2 JP 12592378 A JP12592378 A JP 12592378A JP 12592378 A JP12592378 A JP 12592378A JP S5952681 B2 JPS5952681 B2 JP S5952681B2
- Authority
- JP
- Japan
- Prior art keywords
- floating
- furnace
- floating layer
- layer level
- detection method
- 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
Links
- 238000001514 detection method Methods 0.000 title claims description 6
- 238000009628 steelmaking Methods 0.000 title description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 29
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims description 22
- 239000002994 raw material Substances 0.000 claims description 12
- 229910052742 iron Inorganic materials 0.000 claims description 11
- 239000003575 carbonaceous material Substances 0.000 claims description 5
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 238000000034 method Methods 0.000 description 18
- 238000006722 reduction reaction Methods 0.000 description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 6
- 239000002245 particle Substances 0.000 description 6
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000003245 coal Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
Landscapes
- Manufacture Of Iron (AREA)
Description
【発明の詳細な説明】
本発明は、浮遊式製鉄プロセス(浮遊式直接還元製鉄プ
ロセス)に於ける浮遊層レベル検出方法に関するもので
ある。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a floating layer level detection method in a floating iron making process (floating direct reduction iron making process).
直接製鉄方法にはロータリーキルン法、シャフト炉法及
び流動層法等が知られているが、本発明は流動層法に分
類されるものである。The rotary kiln method, the shaft furnace method, the fluidized bed method, etc. are known as direct iron manufacturing methods, and the present invention is classified into the fluidized bed method.
従来の流動層法では、反応速度が大きい、層内温度が均
一、温度制御が容易等の利点がある反面、熱利用効率が
悪い、粉体(原料)が凝集、付着して操業が困難になる
等の問題点がある。Conventional fluidized bed methods have advantages such as high reaction rate, uniform temperature in the bed, and easy temperature control, but on the other hand, heat utilization efficiency is low and powder (raw materials) aggregates and adheres, making operation difficult. There are problems such as:
最近、これらの問題点を解決する一方法として浮遊式直
接還元製鉄プロセス(浮遊式直接製鉄プロセス)が提案
されている(特願昭51−157726号、等)。Recently, a floating direct reduction iron making process (floating direct iron making process) has been proposed as a method for solving these problems (Japanese Patent Application No. 157726/1983, etc.).
この浮遊式直接製鉄プロセスは、炭素質(石炭、コーク
ス、チャー等)を高温(800〜1000℃)に維持さ
れた炉内に(気体により)浮遊流動させ、炭素質の浮遊
式流動層(浮遊層)を形成し、この層中に酸化鉄原料(
鉄鉱石粉等)を落下させ、層中を通過する間に還元する
プロセスである。This floating direct steelmaking process involves floating carbonaceous material (coal, coke, char, etc.) in a furnace maintained at a high temperature (800-1000°C) (with gas), and creating a carbonaceous floating fluidized bed (floating fluidized bed). layer), and in this layer iron oxide raw material (
This is a process in which iron ore powder, etc.) is dropped and reduced while passing through the layer.
このプロセスの場合、必然的に炉内の流動化流速は、 ○炭素質の浮遊 ○酸化鉄原料の落下 という2つの条件から決ってくる。For this process, the fluidization flow rate in the furnace is necessarily ○Floating carbonaceous matter ○Falling iron oxide raw materials It is determined by two conditions.
従って、これらの条件を満足する流量では炉内浮遊層の
温度を高温に保持するだけの熱量をまかなうことができ
ず、しかも物質収支上必要とされる量としても不足して
くる。Therefore, the flow rate that satisfies these conditions cannot cover the amount of heat sufficient to maintain the temperature of the floating layer in the furnace at a high temperature, and furthermore, the amount required in terms of material balance is insufficient.
そこで、これら2点、つまり
○熱量
○物質収支
をカバーするために、前記炭素質の浮遊層に通電するこ
とにより炭素質を発熱媒体として炉内温度の上昇、更に
、
Fe2O3+3C= 2Fe +3CO
又は
Fe2O3+ 3/2 C= 2Fe + 3/2C0
2の直接還元反応を積極的に促進させ、これによって炉
の生産性を著しく増加させるプロセスが提案されている
(特願昭51−157727号)。Therefore, in order to cover these two points, that is, ○heat amount ○material balance, by supplying electricity to the carbonaceous floating layer, the temperature in the furnace is increased using the carbonaceous material as a heating medium, and furthermore, Fe2O3+3C= 2Fe +3CO or Fe2O3+ 3 /2C=2Fe+3/2C0
A process has been proposed in which the direct reduction reaction of No. 2 is actively promoted, thereby significantly increasing the productivity of the furnace (Japanese Patent Application No. 51-157727).
この浮遊式プロセスにおいては、浮遊層による還元反応
を効率良く行う条件の一つとして浮遊層レベル(層厚)
を迅速に把握することがあげられる。In this floating process, one of the conditions for efficient reduction reaction by the floating layer is the floating layer level (layer thickness).
One example of this is to quickly understand the situation.
そこで本発明者等は種々研究、実験した結果、第1図に
示すように浮遊層の電気抵抗値はある温度以上になると
ほぼ一定であることに着目し、本発明を完成した。As a result of various research and experiments, the inventors of the present invention have completed the present invention by noting that the electrical resistance of the floating layer remains approximately constant above a certain temperature, as shown in FIG.
即ち、本発明は、浮遊層レベルを迅速に且つ容易に検出
でき、浮遊式製鉄プロセスを効率良く運転させることに
寄与せしめることを目的としたもので、炭素質で形成さ
れる浮遊層に酸化鉄原料を投入、沈降させて還元鉄を製
造する浮遊式製鉄プロセスに於いて、炉の複数の高さ位
置で夫々炉内電気抵抗を測定し、該各側定値が予め設定
した規定値であるか否かを判定し、規定値である場合に
その測定高さ位置から浮遊層レベルを求めることを特徴
とする浮遊層レベル検出方法に係るものである。That is, the present invention aims to enable the floating layer level to be detected quickly and easily, and to contribute to the efficient operation of the floating iron making process. In the floating steelmaking process, in which reduced iron is produced by introducing raw materials and allowing them to settle, the electric resistance inside the furnace is measured at multiple heights of the furnace, and the values on each side are determined to be the preset values. The present invention relates to a method for detecting a floating layer level, which is characterized in that the floating layer level is determined from the measured height position when the measured height is a specified value.
以下、図面を参照しつつ本発明の詳細な説明する。Hereinafter, the present invention will be described in detail with reference to the drawings.
第2図は本発明の検出方法を実施するための装置の一例
を概略的に示すものである。FIG. 2 schematically shows an example of an apparatus for carrying out the detection method of the present invention.
1は還元炉(反応塔)であり、該還元炉1の頂部には、
酸化鉄原料(鉄鉱石、酸化ペレット等)A及び炭素質の
一例としての炭素粒体Bを夫々炉内に装入する装入系2
と、炉頂排ガスGを排出する排出系3とが設けである。1 is a reduction furnace (reaction tower), and at the top of the reduction furnace 1,
Charging system 2 in which iron oxide raw material (iron ore, oxide pellets, etc.) A and carbon granules B as an example of carbonaceous material are charged into the furnace, respectively.
and an exhaust system 3 for discharging the furnace top exhaust gas G.
また上記炉1の底部には、予熱(又は加熱)された気体
(還元ガス)Cを炉内に導入する導入系4と、製品とし
て還元鉄り及びチャー(コークス化の前段階のもの)E
を互いに分離させて取り出す抽出系5とが設けである。Further, at the bottom of the furnace 1, there is an introduction system 4 for introducing preheated (or heated) gas (reducing gas) C into the furnace, and reduced iron oxide and char (pre-coking stage) E as products.
An extraction system 5 is provided which separates the two from each other and takes them out.
更に、上記炉1内には、複数対の電極6が炉内壁に沿い
設けである。Furthermore, inside the furnace 1, a plurality of pairs of electrodes 6 are provided along the inner wall of the furnace.
該電極6は、各対の電極が相対向する状態で炉1の高さ
方向に所要間隔をおいて配列されている。The electrodes 6 are arranged at required intervals in the height direction of the furnace 1, with each pair of electrodes facing each other.
本例では例えば5段に配列されており、最上段から順に
、No、 1、No、2、No、3、No、4、No、
5とする。In this example, they are arranged in five rows, starting from the top row: No, 1, No, 2, No, 3, No, 4, No,
5.
各段の電極6,6に結んだ配線の途中には電気抵抗検出
器7が設けてあり、各段の電気抵抗検出器7は、該各検
出器7の測定信号に基づいて判定、演算をして浮遊層レ
ベルを求める演算器8に電気的に結ばれている。An electrical resistance detector 7 is provided in the middle of the wiring connected to the electrodes 6, 6 of each stage, and the electrical resistance detector 7 of each stage performs judgment and calculation based on the measurement signal of each detector 7. It is electrically connected to an arithmetic unit 8 which calculates the floating layer level.
次に、この還元炉1による製鉄プロセスの運転について
述べると、先ず炉の始動期に際しては、予熱(或は加熱
)された還元ガスCを炉内に吹き込むと、この還元ガス
(還元雰囲気)Cは、炉頂から炉頂排ガスGとして排出
され、再度炉内に循環される。Next, to describe the operation of the iron manufacturing process using this reducing furnace 1, first, during the startup period of the furnace, when preheated (or heated) reducing gas C is blown into the furnace, this reducing gas (reducing atmosphere) C is discharged from the furnace top as furnace top exhaust gas G, and is circulated into the furnace again.
この循環を繰り返すことにより循環ガスの還元度は上昇
していく。By repeating this circulation, the degree of reduction of the circulating gas increases.
ここで炉内に予め装入されていた炭素粒体Bが、上記雰
囲気中に浮遊し炉内に炭素粒体Bの浮遊式流動層即ち浮
遊層Fが形成される。Here, the carbon particles B, which had been charged in advance into the furnace, float in the above-mentioned atmosphere, and a floating fluidized bed of carbon particles B, that is, a floating layer F, is formed in the furnace.
次に、電源(図示しない)より電極6,6間に電圧を印
加すると、前記浮遊層Fを形成する炭素粒体Bに通電さ
れ、ジュール熱により炉内温度が上昇する。Next, when a voltage is applied between the electrodes 6 and 6 from a power source (not shown), the carbon particles B forming the floating layer F are energized, and the temperature in the furnace is increased by Joule heat.
この状態で、炉内に酸化鉄原料Aが投入されると、上記
浮遊層Fを通過して降下する。In this state, when the iron oxide raw material A is introduced into the furnace, it passes through the floating layer F and descends.
この酸化鉄原料Aが浮遊層Fを通過する際に、次で示す
還元反応が起こり、酸化鉄原料Aは上記浮遊層Fの一酸
化炭素により還元されつつ、一酸化炭素を含む還元雰囲
気即ち還元ガスが再成される。When this iron oxide raw material A passes through the floating layer F, the following reduction reaction occurs, and the iron oxide raw material A is reduced by the carbon monoxide in the floating layer F, and the iron oxide raw material A is reduced in a reducing atmosphere containing carbon monoxide, that is, reduced. Gas is regenerated.
そして生成した還元鉄りと、チャーEとは分離されて取
り出され、チャーEは炭素粒体として前記装入系2に送
られる。The generated reduced iron oxide and char E are separated and taken out, and the char E is sent to the charging system 2 as carbon particles.
ここで、浮遊層レベル(層厚)の検出方法について説明
する。Here, a method for detecting the floating layer level (layer thickness) will be explained.
前述の還元炉1の運転に際しては、予め実験によりケー
スバイケースに応じた規定の電気抵抗値を求めておく。When operating the above-mentioned reduction furnace 1, a prescribed electrical resistance value is determined in advance based on an experiment on a case-by-case basis.
即ち、第1図は本実施例の場合における炉内の電気抵抗
と温度との関係を示すものであり、約り00℃〜約10
00℃の温度範囲において電気抵抗が一定値R1となっ
ている。That is, FIG. 1 shows the relationship between the electrical resistance and temperature inside the furnace in the case of this example, and it shows the relationship between the electrical resistance and temperature in the furnace, from about 00°C to about 10°C.
The electrical resistance is a constant value R1 in the temperature range of 00°C.
また該浮遊層F上部の温度は通常約り00℃〜約100
0℃であり該層F下部の温度はそれより低くなる。In addition, the temperature at the top of the floating layer F is usually about 00°C to about 100°C.
0° C., and the temperature below the layer F is lower than that.
これは、炭素質(炭素粒体)よりFeの方が電気抵抗値
が大きく、しかも層下部にFeか゛たまり易いため層旧
部が加熱され易いことによる。This is because Fe has a higher electrical resistance value than carbonaceous material (carbon particles), and since Fe tends to accumulate in the lower part of the layer, the old part of the layer is easily heated.
そこで第1図において、抵抗一定区間600℃〜100
0℃に対する電気抵抗値をR1とすると、該R1が規定
値となる。Therefore, in Fig. 1, the constant resistance section is 600°C to 100°C.
If the electrical resistance value at 0° C. is R1, then R1 becomes the specified value.
このようにして求めた電気抵抗の規定値R1を演算器8
に設定しておく。The specified value R1 of the electric resistance obtained in this way is calculated by the calculator 8.
Set it to .
また該演算器8には各段の電極6の高さ値も設定してお
く。Further, the height values of the electrodes 6 at each stage are also set in the calculator 8.
この状態で前述の運転を行うと、運転中、各段の電気抵
抗検出器7により炉内の電気抵抗が測定され、該測定信
号は演算器8に送られる。When the above-mentioned operation is performed in this state, the electrical resistance inside the furnace is measured by the electrical resistance detector 7 at each stage during the operation, and the measurement signal is sent to the computing unit 8.
該演算器8においては、各段からの測定値が前記規定値
R1であるか否かを判定する。The arithmetic unit 8 determines whether the measured value from each stage is the specified value R1.
例えば第2図の場合浮遊層FはNo、1電極6下部に形
成されているから、N001電槙、6間には電流がほと
んど流れず、そのためNo、1の電気抵抗検出器7の夫
々の測定値は前記規定値R1よりも非常に大きな値(は
ぼ無限大)が計測される。For example, in the case of FIG. 2, since the floating layer F is formed under the No. 1 electrode 6, almost no current flows between the No. The measured value is much larger (almost infinite) than the specified value R1.
一方No、5〜N002の電気抵抗測定器7の夫々の測
定値はほは゛同一になり (第1図に示すように浮遊層
一定温度区間600℃以上の場合には電気抵抗値は一定
であるため)しかも前記規定値R1であると判定される
。On the other hand, the measured values of the electrical resistance measuring devices 7 for No. 5 to No. 002 are almost the same (as shown in Figure 1, the electrical resistance values are constant in the floating layer constant temperature range of 600°C or higher). Therefore, it is determined that the value is the specified value R1.
そしてNo、2の電極6の高さ値を演算(上記高さ値の
差を演算)することにより層厚即ち浮遊層レベルが求ま
る(尚上記高さ値の差と層厚との間には若干の誤差が出
る場合もある)。Then, by calculating the height value of the electrode 6 of No. 2 (calculating the difference between the above height values), the layer thickness, that is, the floating layer level can be found (note that the difference between the above height value and the layer thickness is There may be slight errors).
以上述べたように本発明の検出方法は、炉内電気抵抗を
測定することにより浮遊層レベルを検出するので、浮遊
層レベルを迅速に且つ容易に検出でき、これにより炉内
装入物(炭素質、酸化鉄原料)の供給量、供給比率を調
整することが容易且つ正確になり、従って浮遊式製鉄プ
ロセスを効率良く運転させることが可能になる、等の優
れた効果を発揮する。As described above, the detection method of the present invention detects the level of the floating layer by measuring the electric resistance inside the furnace, so the level of the floating layer can be detected quickly and easily. It is easy and accurate to adjust the supply amount and ratio of iron oxide raw materials), and therefore the floating iron making process can be operated efficiently.
第1図は炉内の電気抵抗と温度との関係を示すグラフ、
第2図は本発明の検出方法を実施するための装置の一例
を示す概略図である。
1・・・・・・還元炉、6・・・・・・電極、7・・・
・・・電気抵抗検出器、8・・・・・・演算器、A・・
・・・・酸化鉄原料、B・・・・・・炭素粒体、D・・
・・・・還元鉄、F・・・・・・浮遊層。Figure 1 is a graph showing the relationship between electrical resistance and temperature inside the furnace.
FIG. 2 is a schematic diagram showing an example of an apparatus for carrying out the detection method of the present invention. 1... Reduction furnace, 6... Electrode, 7...
...Electric resistance detector, 8... Arithmetic unit, A...
...Iron oxide raw material, B...Carbon particles, D...
...Reduced iron, F...Floating layer.
Claims (1)
降させて還元鉄を製造する浮遊式製鉄プロセスに於いて
、炉の複数の高さ位置で夫々炉内電気抵抗を測定し、該
各側定値が予め設定した規定値であるか否かを判定し、
規定値である場合にその測定高さ位置から浮遊層レベル
を求めることを特徴とする浮遊層レベル検出方法。1. In the floating iron manufacturing process, in which iron oxide raw materials are introduced into a floating layer formed of carbonaceous material and allowed to settle to produce reduced iron, the electrical resistance inside the furnace is measured at multiple heights of the furnace, and the Determine whether each side fixed value is a preset specified value,
A floating layer level detection method characterized by determining the floating layer level from the measured height position when it is a specified value.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12592378A JPS5952681B2 (en) | 1978-10-13 | 1978-10-13 | Floating layer level detection method in floating steelmaking process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12592378A JPS5952681B2 (en) | 1978-10-13 | 1978-10-13 | Floating layer level detection method in floating steelmaking process |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5554516A JPS5554516A (en) | 1980-04-21 |
| JPS5952681B2 true JPS5952681B2 (en) | 1984-12-21 |
Family
ID=14922284
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12592378A Expired JPS5952681B2 (en) | 1978-10-13 | 1978-10-13 | Floating layer level detection method in floating steelmaking process |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5952681B2 (en) |
-
1978
- 1978-10-13 JP JP12592378A patent/JPS5952681B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5554516A (en) | 1980-04-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4224056A (en) | Direct reduction process for iron ores with fluidized bed system | |
| US4140301A (en) | Method and apparatus for reducing particulate iron oxide to metallic iron with solid reductant | |
| CA1224516A (en) | Electric arc fired cupola for remelting of metal chips | |
| US4025610A (en) | Method and apparatus for denitrifying coke | |
| US4158695A (en) | Electrothermal fluidized bed furnace | |
| JPS5952681B2 (en) | Floating layer level detection method in floating steelmaking process | |
| US2744944A (en) | Rotating electric phosphorus furnace | |
| US2840458A (en) | Heating finely divided solid reactants | |
| US1430971A (en) | Method of and means for reducing ores in electric blast furnaces | |
| CN116304492B (en) | Calculation method of temperature distribution in roasting process of self-roasting electrode of direct-current submerged arc furnace | |
| WO1998038130A1 (en) | Operation management method of iron carbide production process | |
| JPS5943963B2 (en) | How to control floating reduction process | |
| US1917942A (en) | Method and apparatus for heat treatment of materials in rotary furnaces | |
| Mostert, JC* & Roberts | Electric smelting at Rustenburg Platinum Mines Limited of nickel-copper concentrates containing platinum-group metals | |
| US4195821A (en) | Apparatus for reducing particulate iron oxide to molten iron with solid reductant | |
| JPS6014807B2 (en) | Temperature control method for floating steelmaking process | |
| JPS6014806B2 (en) | How to control floating reduction process | |
| JPS6014805B2 (en) | How to control floating reduction process | |
| US826743A (en) | Process of reducing compounds and producing carbids. | |
| JPH0280491A (en) | Operation of continuous formed coke oven | |
| US757634A (en) | Electric-resistance furnace. | |
| JPS5948924B2 (en) | Electrical heating method for floating steelmaking process | |
| JPS5544517A (en) | Heating method of floating type iron making process | |
| CN202220082U (en) | Rectangular electric calcining device and calcining tray furnace thereof | |
| US794255A (en) | Electric furnace. |