JPH01316429A - Method for manufacturing sintered ore - Google Patents
Method for manufacturing sintered oreInfo
- Publication number
- JPH01316429A JPH01316429A JP14481688A JP14481688A JPH01316429A JP H01316429 A JPH01316429 A JP H01316429A JP 14481688 A JP14481688 A JP 14481688A JP 14481688 A JP14481688 A JP 14481688A JP H01316429 A JPH01316429 A JP H01316429A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust
- sintering
- exhaust system
- exhaust gas
- amt
- 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.)
- Pending
Links
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
【発明の詳細な説明】
〈産業上の利用分野〉
この発明は、焼結鉱の品質や操業性に悪影響を及ぼすこ
となく焼結機排気系の排ガス温度を制御し、良好な装置
環境を維持しながら高品質の焼結鉱を安定に製造するた
めの方法に関するものである。[Detailed Description of the Invention] <Industrial Application Field> This invention controls the exhaust gas temperature of the sintering machine exhaust system without adversely affecting the quality of sintered ore or the operability, and maintains a good equipment environment. The present invention relates to a method for stably producing high-quality sintered ore.
〈従来技術とその課題〉
現在、高炉等で使用する原料鉱石の塊状化はドワイトロ
イド式焼結機によって行われるのが一般的であるが、こ
のドワイトロイド式焼結機による焼結鉱の製造はほぼ第
2図で示すような形態で実施されている。即ち、第2図
において、焼結機1の原料給鉱部ヘホッパ2から装入さ
れた焼結配合原料3はカントプレート4にて厚さ調整が
なされた後、点火炉5にて表面より着火され、原料収容
パレットの移動方向に沿って併設された排風機6により
燃焼帯7が下方に吸引される。そして、この排風機6に
よる下向きの通風によって焼成反応が装入原料の下層に
向かって進行し、排鉱部では高さ方向の全てにわたって
焼成が完了することとなり、焼結ケーキが形成される。<Prior art and its problems> Currently, the agglomeration of raw material ore used in blast furnaces, etc. is generally performed using a Dwight Lloyd sintering machine. is implemented approximately in the form shown in FIG. That is, in FIG. 2, the sintering compound raw material 3 charged from the hopper 2 to the raw material feeding section of the sintering machine 1 is adjusted in thickness with the cant plate 4, and then ignited from the surface in the ignition furnace 5. The combustion zone 7 is sucked downward by the exhaust fan 6 provided along the moving direction of the raw material storage pallet. Then, the sintering reaction progresses toward the lower layer of the charged material due to the downward ventilation by the exhaust fan 6, and sintering is completed in the entire height direction in the ore discharge section, forming a sintered cake.
ところで、上記のような焼結作業においては、通常、焼
結機排ガスの顕熱回収や排ガス量の削減を目的として燃
焼帯を下方に吸引するためのガス吸引用排気系を機長方
向に複数分割し、排ガスの一部を再循環させることが行
われている。例えば、最も一般的には、第3図で略示す
るように排気系を機長方向に二分割し、後半部の排気系
(循環排風機8が設置されている)にボイラーを組み込
んで排ガスから排熱回収を行った後、その排ガスを再循
環させる等の平文てが講じられている。By the way, in the above-mentioned sintering work, the gas suction exhaust system for sucking the combustion zone downward is usually divided into multiple parts in the longitudinal direction for the purpose of recovering sensible heat from the sintering machine exhaust gas and reducing the amount of exhaust gas. However, some of the exhaust gas is recirculated. For example, most commonly, the exhaust system is divided into two parts in the longitudinal direction, as schematically shown in Figure 3, and a boiler is installed in the rear exhaust system (where the circulation exhaust fan 8 is installed) to remove exhaust gas. Measures are being taken to recirculate the exhaust gas after recovering the exhaust heat.
ところが、このようなプロセスにおいては、比較的高温
の排ガスが回収される後半部の排気系では問題がないも
のの、前半部の主排気系(主排風機9が設置されている
)では排ガスの温度が低下し易いため酸腐食が問題とな
っていた。つまり、排ガスの温度が後半部の排気系に比
して低くなりがちな主排気系においては、排ガス温度が
酸露点を下回ってしまうことがあり、このため結露し主
排気系に付着した酸によって該主排気系が腐食を受ける
との報告が見られたからである。なお、図面において、
符号10.10”はフードを示している。However, in such a process, although there is no problem in the exhaust system in the second half where relatively high-temperature exhaust gas is recovered, in the main exhaust system in the first half (where the main exhaust fan 9 is installed), the temperature of the exhaust gas is low. Acid corrosion has been a problem since it tends to deteriorate. In other words, in the main exhaust system, where the temperature of the exhaust gas tends to be lower than that of the exhaust system in the latter half, the exhaust gas temperature may fall below the acid dew point, and as a result, dew condensation and acid adhering to the main exhaust system cause the exhaust gas temperature to drop below the acid dew point. This is because there have been reports that the main exhaust system is subject to corrosion. In addition, in the drawing,
Reference numeral 10.10'' indicates a hood.
そこで、上述のような腐食問題に対処するため、従来は
、主排気系の排ガス温度の下限目標値を酸露点以上の温
度に定めた上で、主排風量の調整や原料を装入したパレ
ットの速度調整によって焼成完了点(B T P)を変
更させ、これにより主排気系の排ガス温度が前記設定値
を満足するように温度管理する対策が採られていた。Therefore, in order to deal with the above-mentioned corrosion problem, conventionally, the lower target value of the exhaust gas temperature of the main exhaust system was set at a temperature higher than the acid dew point, and the main exhaust air volume was adjusted and the pallet charged with raw materials was Measures have been taken to change the firing completion point (BTP) by adjusting the speed of , thereby controlling the temperature so that the exhaust gas temperature of the main exhaust system satisfies the set value.
即ち、第3図の下部に示すグラフは、その上部に略示す
る焼結機排気系における排ガスの温度パターン例であり
、定常操業状態では一点鎖線で示されるようなベース形
態をとっているものとする。That is, the graph shown at the bottom of Fig. 3 is an example of the temperature pattern of the exhaust gas in the sintering machine exhaust system, which is schematically shown at the top, and under steady operating conditions, it takes the base form as shown by the dashed line. shall be.
ここで、主排気系の排ガス温度(T1)が低下傾向を示
した場合に、該温度を上昇させて所定温度を確保すべく
主排気系の排風量(Ql)を増加すると、排気系の排ガ
スは実線Aで示すような温度パターンとなってBTPは
主排気系寄りのBTP ’の位置へ変化し、主排気系に
吸引される高温の排ガス割合が増すので、主排気系の排
ガス温度は上昇することとなる。なお、主排気系の排風
量を増加させることに代えてパレットの移動速度を遅く
しても同様の効果が得られる。Here, when the exhaust gas temperature (T1) of the main exhaust system shows a decreasing tendency, if the exhaust air volume (Ql) of the main exhaust system is increased in order to raise the temperature and secure a predetermined temperature, the exhaust gas temperature of the exhaust system becomes the temperature pattern shown by solid line A, and BTP changes to the position of BTP', which is closer to the main exhaust system, and the proportion of high-temperature exhaust gas sucked into the main exhaust system increases, so the exhaust gas temperature in the main exhaust system rises. I will do it. Note that the same effect can be obtained by slowing down the moving speed of the pallet instead of increasing the amount of air exhausted from the main exhaust system.
そして、この場合、排ガス温度を必要以上に上げること
は排風機電力の無駄であり、また排熱回収量も減少する
ことから避けるべきであるとされていた。In this case, it was considered that raising the exhaust gas temperature more than necessary was a waste of electric power for the exhaust fan and should be avoided since it would also reduce the amount of exhaust heat recovered.
しかしながら、主排気系の排ガス温度は外気温の変化や
主排気系の漏風等に敏感に影響されるものであるためそ
の温度調整は比較的頻繁に行う必要があったが、排ガス
温度を一定に保つべく上記の如きBTP位置の変更を行
った場合には、操業の変動幅が増大することは勿論、焼
結鉱の品質変動も大きくなって好ましくないとの事実が
明らかとなった。However, since the exhaust gas temperature in the main exhaust system is sensitive to changes in outside temperature and air leakage in the main exhaust system, it was necessary to adjust the temperature relatively frequently. It has become clear that if the BTP position is changed as described above in order to maintain the same, the fluctuation range of the operation will not only increase, but also the quality fluctuation of the sintered ore will also increase, which is not desirable.
そこで、本発明の主目的は、焼結鉱の製造に際して指摘
される前記問題点を解消し、操業状況や焼結鉱品質の変
動を極力抑制しつつ排ガス温度を一定に管理することに
よって、良好な装置環境を維持しながら高品質の焼結鉱
を安定に製造し得る手段を提供することにある。Therefore, the main purpose of the present invention is to solve the above-mentioned problems pointed out in the production of sintered ore, and to control the exhaust gas temperature at a constant level while suppressing fluctuations in operating conditions and sintered ore quality as much as possible. The object of the present invention is to provide a means for stably producing high-quality sintered ore while maintaining a suitable equipment environment.
〈課題を解決するための手段〉
本発明者等は、上記目的を達成すべく様々な観点から鋭
意研究を行ったところ、[ガス吸引用の排気系を機長方
向に複数分割した焼結機においては、主排気系の風量を
増加して主排ガス温度を上昇させた場合、それに見合う
熱量分だけ循環排気系の風量・温度を下げるとBTP位
置の変動が抑制でき、主排気系の排ガス温度を所定値に
維持しつつ安定な操業条件下で品質の良好な焼結鉱が得
られるようになる」との知見を得るに至ったのである。<Means for Solving the Problems> The present inventors conducted intensive research from various viewpoints in order to achieve the above object, and found that [In a sintering machine in which the exhaust system for gas suction is divided into multiple parts in the machine length direction] In this case, when the main exhaust gas temperature is increased by increasing the air volume of the main exhaust system, the fluctuation of the BTP position can be suppressed by lowering the air volume and temperature of the circulating exhaust system by the corresponding amount of heat, and the exhaust gas temperature of the main exhaust system can be reduced. They came to the conclusion that sintered ore of good quality can be obtained under stable operating conditions while maintaining the specified value.
本発明は、上記知見等に基づいてなされたものであり、
「ガス吸引用の排気系を機長方向に複数分割した焼結機
で焼結鉱を製造するに際して、焼結機主排気系の排風量
変動に呼応させて循環排風機の風量を調整し、これによ
ってBTPの位置変動を抑えつつ焼成を行うことにより
、良好な装置環境を維持しながら品質の安定した焼結鉱
を作業性良く製造し得るようにした点」
に特徴を有するものである。The present invention has been made based on the above-mentioned findings and the like. By adjusting the air volume of the circulation exhaust fan in response to air volume fluctuations and performing firing while suppressing BTP position fluctuations, we can produce sintered ore of stable quality with good workability while maintaining a good equipment environment. It is characterized by the fact that it has been made possible to
即ち、本発明は、機長方向へ複数に分割された排気系を
有する焼結機の定常時での排気系各部の排ガス温度を計
測し、そのときの排ガス温度パターンを把握しておき、
主排気系における排ガス温度に変動の兆しが見える場合
には、焼結機主排風機の吸引風量の調整により、かつ該
主排風機の吸引風量と循環排風機吸引風量比率を調整し
て前記温度パターンをほぼ維持させつつ主排気系の排ガ
ス温度を一定に保持し、焼結鉱品質の安定化を図るもの
であるが、以下、第1図を参照しながら本発明を説明す
る。That is, the present invention measures the exhaust gas temperature of each part of the exhaust system during steady state of a sintering machine having an exhaust system divided into a plurality of parts in the longitudinal direction, and grasps the exhaust gas temperature pattern at that time.
If there are signs of fluctuations in the exhaust gas temperature in the main exhaust system, adjust the suction air volume of the sintering machine main exhaust fan, and adjust the suction air volume of the main exhaust fan and the circulation exhaust fan suction air volume ratio to increase the temperature. The present invention is intended to stabilize the quality of sintered ore by keeping the exhaust gas temperature of the main exhaust system constant while substantially maintaining the pattern.Hereinafter, the present invention will be explained with reference to FIG. 1.
第1図は、排気系を機長方向に二分割した焼結機による
本発明法の適用例を示した説明図であるが、上記焼結機
において主排風機9系の温度(T1)を上昇させるには
、その風量(Q、)を増加させるのが最も効果的で簡便
な手段であるが、この場合には、前述したように第3図
の実線Aの如き焼成温度パターン(排気系の排ガス温度
パターン)となり、BTP位置が変化してしまう。Figure 1 is an explanatory diagram showing an example of application of the method of the present invention using a sintering machine in which the exhaust system is divided into two in the machine length direction. The most effective and simple way to achieve this is to increase the air volume (Q), but in this case, as mentioned above, the firing temperature pattern (exhaust system (exhaust gas temperature pattern), and the BTP position changes.
ところが、主排風機9系の風量(Ql)を増加させて該
主排風機9系の温度上昇を図る場合であっても、本発明
に従って排風機9系の排ガス熱量変化に相当する分だし
)循環排風機8系の風量(Ch)。However, even in the case where the temperature of the main exhaust fan 9 system is increased by increasing the air volume (Ql) of the main exhaust fan 9 system, according to the present invention, the change is equivalent to the change in exhaust gas heat amount of the exhaust fan 9 system) Air volume (Ch) of circulation exhaust fan 8 system.
温度(T2)を変更することにより、即ちΔT2×ΔQ
2’ (ΔT1×ΔQl)となるように循環排風機
8の風量を調整することにより、第1図で示す如く、ベ
ースパターンからBTP位置が殆んど変化しない実線B
のような焼成温度パターン(排気系め排ガス温度パター
ン)で焼結を実施できることとなり、操業や品質の安定
化が実現できるわけである。By changing the temperature (T2), i.e. ΔT2×ΔQ
2' (ΔT1×ΔQl), by adjusting the air volume of the circulation exhaust fan 8, as shown in FIG.
This means that sintering can be carried out with a sintering temperature pattern (exhaust gas temperature pattern from the exhaust system) such as this, making it possible to stabilize operations and quality.
続いて、本発明を実施例によって具体的に説明する。Next, the present invention will be specifically explained using examples.
〈実施例〉
機長60mの排気系を5:1に二分割し、ボイラーにて
後半部で吸引した排ガスから排熱回収した後再循環させ
るタイプの第1図に略示したようなドワイトロイド式焼
結機を使用して、各種排気条件の下で粉鉄鉱石の焼結実
験を行った。<Example> Dwight Lloyd type, as schematically shown in Figure 1, in which the exhaust system with a length of 60 m is divided into two parts at a ratio of 5:1, exhaust heat is recovered from the exhaust gas sucked into the latter half by the boiler, and then recirculated. Sintering experiments of fine iron ore were conducted using a sintering machine under various exhaust conditions.
なお、この場合の排ガスの露点は約65℃であるので、
主排気系各部の温度をそれ以上に管理するためには主排
風機9人口における排ガス温度を85℃に管理すること
が必要であった。In addition, since the dew point of the exhaust gas in this case is approximately 65°C,
In order to control the temperature of each part of the main exhaust system above that level, it was necessary to control the exhaust gas temperature at 85° C. in the nine main exhaust fans.
このように主排風機9人口における排ガス温度を85℃
に維持しながら粉鉄鉱石の焼成を行ったときの操業状況
を第1表に示す。In this way, the exhaust gas temperature at the main exhaust fan 9 is set at 85℃.
Table 1 shows the operating conditions when calcination of fine iron ore was carried out while maintaining the following conditions.
第 1 表
なお、第1表において、「ベース」は定常状態の操業を
、また「従来法」は主排風量を高めるのみで主排風機9
人口における排ガス温度を所定値に維持した場合を、そ
して「本発明法」はΔT2×ΔQz= (ΔT、XΔ
Q l )の関係に従って排気条件を調整することによ
り主排風機9人口における排ガス温度を所定値に維持し
た場合をそれぞれ意味している。Table 1 In Table 1, ``Base'' refers to steady state operation, and ``Conventional method'' refers to only increasing the main exhaust air volume.
In the case where the exhaust gas temperature in the population is maintained at a predetermined value, the "method of the present invention" is ΔT2×ΔQz= (ΔT, XΔ
This means the case where the exhaust gas temperature at the main exhaust fan 9 is maintained at a predetermined value by adjusting the exhaust conditions according to the relationship Q l ).
第1表に示される結果からも明らかなように、従来法で
は、BTPの移動(焼成速度増加)により還元粉化性は
改善されるものの回転強度が低下し、また排風機の電力
使用量が増加することが分かる。As is clear from the results shown in Table 1, in the conventional method, the reduction and powdering properties are improved due to the movement of BTP (increased firing speed), but the rotational strength is reduced, and the power consumption of the exhaust fan is reduced. It can be seen that it increases.
これに対して、本発明法によるとBTP位置がほぼ一定
であり、焼結鉱品質の変化が少な゛くて電力使用量もほ
ぼ一定となる良好な結果がもたらされたことが確認でき
る。On the other hand, it can be confirmed that the method of the present invention has brought about good results in which the BTP position is almost constant, there is little change in the quality of the sintered ore, and the amount of electricity used is also almost constant.
〈効果の総括〉
以上に説明した如く、この発明によれば、操業や製品品
質の安定性を損なうことなく主排気系の排ガス温度を一
定値に維持し、排気系の酸腐食を有効に抑えながら品質
の良好な焼結鉱をコスト安く安定製造することが可能と
なるなど、産業上有用な効果がもたらされる。<Summary of Effects> As explained above, according to the present invention, the exhaust gas temperature in the main exhaust system can be maintained at a constant value without impairing the stability of operation or product quality, and acid corrosion in the exhaust system can be effectively suppressed. However, industrially useful effects are brought about, such as making it possible to stably produce high-quality sintered ore at low cost.
第1図は、排気系を機長方向に二分割した焼結機による
本発明法の適用例を示した説明図である。
第2図は、ドワイトロイド式焼結機による焼結操業状況
を示す概念図である。
第3図は、排気系を機長方向に二分割した焼結機による
従来法の適用例を示した説明図である。
図面において、
1・・・焼結機、 2・・・ホッパー。
3・・・焼結配合原料、 4・・・カフ)プレート
。
5・・・点火炉、 6・・・排風機。
7・・・燃焼帯、 8・・・循環排風機。
9・・・主排風機、 10.10′・・・フー
ド。FIG. 1 is an explanatory diagram showing an example of application of the method of the present invention using a sintering machine in which the exhaust system is divided into two in the longitudinal direction. FIG. 2 is a conceptual diagram showing the sintering operation status using the Dwight Lloyd sintering machine. FIG. 3 is an explanatory diagram showing an example of application of the conventional method using a sintering machine in which the exhaust system is divided into two in the longitudinal direction. In the drawings: 1...Sintering machine, 2...Hopper. 3...Sintering compound raw material, 4...Cuff) plate. 5... Ignition furnace, 6... Exhaust fan. 7... Combustion zone, 8... Circulation exhaust fan. 9... Main exhaust fan, 10.10'... Hood.
Claims (1)
焼結鉱を製造するに際して、焼結機主排気系の排風量変
動に呼応させて循環排風機の風量を調整し、これによっ
て焼成完了点の位置変動を抑えつつ焼成を行うことを特
徴とする焼結鉱の製造方法。When producing sintered ore using a sintering machine in which the exhaust system for gas suction is divided into multiple parts in the machine length direction, the air volume of the circulation exhaust fan is adjusted in response to fluctuations in the exhaust air volume of the sintering machine's main exhaust system. A method for producing sintered ore, characterized by performing firing while suppressing positional fluctuations of the firing completion point.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14481688A JPH01316429A (en) | 1988-06-14 | 1988-06-14 | Method for manufacturing sintered ore |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14481688A JPH01316429A (en) | 1988-06-14 | 1988-06-14 | Method for manufacturing sintered ore |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH01316429A true JPH01316429A (en) | 1989-12-21 |
Family
ID=15371129
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14481688A Pending JPH01316429A (en) | 1988-06-14 | 1988-06-14 | Method for manufacturing sintered ore |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH01316429A (en) |
-
1988
- 1988-06-14 JP JP14481688A patent/JPH01316429A/en active Pending
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