JPS5831374B2 - Mixing method of sintering raw materials - Google Patents
Mixing method of sintering raw materialsInfo
- Publication number
- JPS5831374B2 JPS5831374B2 JP5478281A JP5478281A JPS5831374B2 JP S5831374 B2 JPS5831374 B2 JP S5831374B2 JP 5478281 A JP5478281 A JP 5478281A JP 5478281 A JP5478281 A JP 5478281A JP S5831374 B2 JPS5831374 B2 JP S5831374B2
- Authority
- JP
- Japan
- Prior art keywords
- amount
- coke
- raw material
- added
- coke powder
- 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
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
【発明の詳細な説明】
この発明は、焼結原料に混合されるコークス等の固体燃
料の添加量を原料ね度に基づいて制御することにより、
焼結過程での燃焼効率並びに品質の向上をはかる焼結原
料の配合方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention has the following advantages: By controlling the amount of solid fuel such as coke mixed into the sintering raw material based on the raw material sonicity,
This invention relates to a method of blending sintering raw materials to improve combustion efficiency and quality during the sintering process.
焼結原料に配合される固体燃料としては、普通、粉コー
クスが使用されるが、この粉コークスは従来、他の原料
と同時に切出し、ミキサで混合している。Coke powder is usually used as a solid fuel to be mixed into the sintering raw material, but this coke powder is conventionally cut out at the same time as other raw materials and mixed in a mixer.
ところが、粉コークスを他の原料および水分と同時に混
合する方法では、擬似粒化された個個の粒子内に粉コー
クスが混入し個々の擬似粒子の表層に付着する量が少な
く、焼結過程での燃焼効率の悪化をきたす。However, in the method of mixing coke powder with other raw materials and water at the same time, the coke powder gets mixed into the individual pseudo-granules, and the amount of coke powder that adheres to the surface layer of each pseudo-granule is small, causing problems during the sintering process. This causes deterioration of combustion efficiency.
燃焼効率が悪化すると、当然成品焼結鉱の品質も向上し
ないため、従来の方法では粉コークスの添加量を増加さ
せなければならなかった。If the combustion efficiency deteriorates, the quality of the finished sintered ore naturally does not improve, so in the conventional method, it was necessary to increase the amount of coke breeze added.
また、焼結原料に粉コークスを添加する場合、粉コーク
スの添加量は焼結鉱の品質と大きく関係するため、その
添加制御は適確に行なう必要がある。Furthermore, when coke powder is added to the sintering raw material, the amount of coke powder added is greatly related to the quality of the sintered ore, so the addition must be controlled accurately.
その方法として、従来は成品焼結鉱の強度、還元粉化率
等品質を実測し、この実測値に基づいて粉コークスの添
加量を制御している。Conventionally, this method involves actually measuring the quality of the finished sintered ore, such as its strength and reduction pulverization rate, and controlling the amount of coke breeze added based on these measured values.
しかし、この方法では、原料粒度および擬似粒度が異な
るために適正コークス量の添加が難しく、また添加アク
ションの時間的ずれにより焼結鉱品質のばらつきが大き
く、品質の安定した焼結鉱の製造が困難であった。However, with this method, it is difficult to add an appropriate amount of coke due to the difference in raw material particle size and pseudo-particle size, and the time lag in the addition action causes large variations in sinter quality, making it difficult to produce sinter with stable quality. It was difficult.
この発明は、従来の前記問題を解消するためになされた
もので、より適確に粉コークスを配合し得る方法を提案
することを目的とする。This invention was made in order to solve the above-mentioned conventional problems, and aims to propose a method of blending coke powder more accurately.
この発明の要旨は、コークス等固体燃料を含まない焼結
配合原料に所定量の水分を添加して混練し、予め定めた
通気度とコークス等固体燃料添加量との関係から、前記
混練配合原料の実測通気度に応じて所定量のコークス等
固体燃料を添加混合することを特徴とする焼結原料の配
合方法である。The gist of this invention is to add a predetermined amount of moisture to a sintered blended raw material that does not contain solid fuel such as coke and knead it, and from the relationship between the predetermined air permeability and the amount of solid fuel such as coke added, the kneaded blended raw material This method of blending raw materials for sintering is characterized by adding and mixing a predetermined amount of solid fuel such as coke according to the measured air permeability of the sintering material.
すなわち、この発明は、原料と燃料(以下粉コークスで
代表する)を同時混合する際、造粒していく過程におい
て疑似粒子内にコークスが混入するのを防止するため、
焼結原料を擬似粒化する過程での混練を、粉コークスを
含有しない焼結原料と水分のみとし、疑似粒化後に粉コ
ークスを添加する方法をとったのである。That is, in order to prevent coke from being mixed into pseudo particles during the granulation process when raw materials and fuel (hereinafter represented by coke powder) are simultaneously mixed,
In the process of pseudo-granulating the sintered raw material, only the sintering raw material containing no coke powder and water are kneaded, and the coke powder is added after the pseudo-granulation.
さらに、原料粒度および擬似粒度が異なる点を考慮して
、擬似粒化後における粉コークス添加量は、予め定めた
通気度と粉コークス添加量との関係から、擬似ね化後の
実測通気度に応じて定まる方法をとったのである。Furthermore, taking into account the difference in raw material particle size and pseudo-granularity, the amount of coke breeze added after pseudo-granulation is determined based on the relationship between the predetermined air permeability and the amount of coke breeze added, and the amount of coke breeze added after pseudo-granulation is adjusted to the actual air permeability after pseudo-negativity. The method was determined accordingly.
なお、この発明法において、擬似ね化後の実測通気度に
対応する粉コークス添加量を求めるための、通気度と粉
コークス添加量との関係は、水分−足下での粉コークス
を含有しない配合原料のミキサ−による混練後の通気度
を測定し、該測定値より粉コークス添加量を求めるもの
で、その関係は例えば第1図に示すような図表で表わす
ことができる。In addition, in this invention method, the relationship between the permeability and the amount of coke breeze added in order to find the amount of coke breeze added corresponding to the measured air permeability after pseudo-negation is based on the relationship between the moisture content and the amount of coke breeze added at the bottom. The air permeability of the raw materials after kneading with a mixer is measured, and the amount of coke powder added is determined from the measured value, and the relationship can be expressed, for example, in a diagram as shown in FIG.
すなわち、この図表から、混練後の通気度が小の場合は
、当然のことながら擬似粒化された個々の粒子が小さい
ため、粉コークスの添加量は少なくて済み、通気度が犬
となるにしたかつて粉コークスの添加量は多くしなけれ
ばならないことがわかる。In other words, from this chart, when the air permeability after kneading is small, the individual pseudo-granulated particles are of course small, so the amount of coke powder added is small, and the air permeability is small. It can be seen that the amount of coke powder added must be increased.
従って、このような図表を用いた場合には、実測通気度
に対応する粉コークス添加量を読みとって混線後の配合
原料に添加することにより、適正コークス量で擬似粒化
された粒子の表層にまんべんなく粉コークスを付着させ
ることかできる。Therefore, when such a chart is used, by reading the amount of coke powder added corresponding to the measured air permeability and adding it to the blended raw material after cross-talk, the appropriate coke amount can be added to the surface layer of the pseudo-granulated particles. It is possible to apply powdered coke evenly.
この発明法によれは、原料粒度および擬似ね度に適応し
たコークス添加であるため、常に適正コクス量を添加混
合することができ、よって焼結過程における燃焼効率は
極めて高いものとなり品質良好な焼結鉱が得られる。According to the method of this invention, since the coke addition is adapted to the raw material particle size and pseudo-hardness, the appropriate amount of coke can always be added and mixed, and therefore the combustion efficiency in the sintering process is extremely high, resulting in good quality sintering. Concretion is obtained.
また、粉コークスを含有しない混練配合原料の実測通気
度に応じて粉コークスを添加するので、成品焼結鉱の品
質に基づいて粉コークスの添加量を制御する従来法にお
けるような制御性の遅れがなく、品質のばらつきを著し
く軽減させることができる。In addition, since coke powder is added according to the measured air permeability of the mixed raw materials that do not contain coke powder, there is a delay in controllability compared to the conventional method in which the amount of coke powder added is controlled based on the quality of the finished sintered ore. There is no difference in quality, and the variation in quality can be significantly reduced.
次に、この発明法を実施するための装置の一例を第2図
に基づいて説明する。Next, an example of an apparatus for carrying out the method of this invention will be explained based on FIG. 2.
1は原料槽、2は搬送コンベヤー、3は1次ミキサー、
4は配合原料ホッパー、5は搬送コンベヤー、6は粉コ
ークスホッパー、7は水分供給管、8は注水量制御装置
、9は水分計、10は通気度計、11は粉コークス添加
量演算装置、12は配合原料通気度と粉コークス添加量
の関係を設定する設定器、13は粉コークス切出し制御
装置をそれぞれ示す。1 is a raw material tank, 2 is a conveyor, 3 is a primary mixer,
4 is a mixed raw material hopper, 5 is a conveyor, 6 is a coke powder hopper, 7 is a water supply pipe, 8 is a water injection amount control device, 9 is a moisture meter, 10 is an air permeability meter, 11 is a coke powder addition amount calculation device, Reference numeral 12 indicates a setting device for setting the relationship between the air permeability of the blended raw materials and the amount of coke breeze added, and 13 indicates a coke breeze cutting control device.
すなわち、原料槽1から切出された各焼結原料は、搬送
コンベヤー2を介して1次ミキサー3へ送られ、水分供
給管7より供給される水分と混練される。That is, each sintered raw material cut out from the raw material tank 1 is sent to the primary mixer 3 via the conveyor 2 and kneaded with moisture supplied from the moisture supply pipe 7.
この混練配合原料は次の原料ホッパー4に投入され、通
気度計10により該ホッパー内通気度を測定する。The kneaded and blended raw materials are put into the next raw material hopper 4, and the air permeability in the hopper is measured using an air permeability meter 10.
この実測通気度を粉コークス添加量演算装置11に入力
し、前記設定器12に予め入力されている通気度−粉コ
ークス添加量の関係より前記実測通気度に対応する粉コ
ークス添加量を求め、その値に応じて粉コークス切出し
制御装置13により粉コークスを切出し、原料ホッパー
4より切出され搬送コンベヤー5を流れる混練配合原料
に添加する。Inputting this measured air permeability into the coke breeze addition amount calculating device 11, and determining the amount of coke breeze addition corresponding to the measured air permeability from the relationship between air permeability and coke breeze addition amount that has been input in advance into the setting device 12; According to the value, coke powder is cut out by the coke powder cutting control device 13 and added to the kneaded blended raw material cut out from the raw material hopper 4 and flowing through the conveyor 5.
前記粉コークス添加後の原料は二次ミキサーで再混練さ
れて焼結機に装入される。The raw material after the addition of coke powder is kneaded again in a secondary mixer and charged into a sintering machine.
なお、各焼結原料に水分を添加して1次ミキサ3により
混練する際、1次ミキサー内の配合原料水分を一定に保
つため水分計9により水分測定し、注水量制御装置8に
より水分の添加制御を行なう。When adding water to each sintered raw material and kneading it in the primary mixer 3, the water content is measured with a moisture meter 9 in order to keep the water content of the blended raw materials in the primary mixer constant, and the water content is controlled by the water injection amount control device 8. Perform addition control.
以下、この発明の実施例について説明する。Examples of the present invention will be described below.
第1表に示す配合割合を有する粉コークスを含有しない
原料に同第1表に示す量の水分を添加してミキサーによ
り混練し、該混線原料の通気度を測定し、予め定めた通
気度−粉コークス添加量の関係から前記実測通気度に対
応する粉コークス添加量として、第1表に示す量の粉コ
ークスを前記混練原料に添加混合した焼結配合原料を焼
結試験鋼にて焼結した。Water in the amount shown in Table 1 is added to the raw material not containing coke powder having the blending ratio shown in Table 1, and the mixture is kneaded with a mixer.The permeability of the mixed raw material is measured, and the air permeability - Based on the relationship between the amount of coke powder added and the amount of coke powder added corresponding to the measured air permeability, the amount of coke powder shown in Table 1 was added to the kneaded raw material and mixed, and the sintered blended raw material was sintered using a sintering test steel. did.
そのときの焼成条件は第2表に示し、得られた成品焼結
鉱の品質は第3表に示す。The firing conditions at that time are shown in Table 2, and the quality of the obtained sintered ore is shown in Table 3.
なお、第3表には比較のため、第1表に示す原料、粉コ
ークス、水分を同時に添加混合したものについて、同一
の焼成条件で焼結して得られた従来法による焼結鉱の品
質を併記した。For comparison, Table 3 shows the quality of sintered ore obtained by the conventional method obtained by sintering the raw materials shown in Table 1, coke powder, and water simultaneously under the same firing conditions. Also listed.
第3表の結果より明らかなごとく、この発明法によれば
、原料、粉コークスおよび水分を同時に混練する従来法
による焼結鉱より良好な品質の焼結鉱が得られるととも
に、品質のばらつきも少ない。As is clear from the results in Table 3, according to the method of this invention, sintered ore of better quality can be obtained than the sintered ore produced by the conventional method of kneading raw materials, coke powder, and water at the same time, and the variation in quality is also reduced. few.
従って、この発明は焼結鉱の品質向上ならびに燃料原単
位の低減に犬なる効果を奏するとともに、生産性の向上
も期待できる。Therefore, this invention has significant effects on improving the quality of sintered ore and reducing fuel consumption, and can also be expected to improve productivity.
第1図はこの発明における原料通気度と粉コークス添加
量の関係の一例を示す図表、第2図はこの発明法を実施
するための装置の一例を示す説明図である。
1・・・原料槽、2,5・・・搬送コンベヤー 3・・
・−次ミキサ−4・・・配合原料ホンパー 6・・・粉
コークスホッパー、7・・・水分供給管、8・・・注水
量制御装置、9・・・水分計、10・・・通気度計、1
1・・・粉コークス添加量演算装置、12・・・設定器
、13・・・粉コークス切出し制御装島FIG. 1 is a chart showing an example of the relationship between raw material permeability and the amount of coke powder added in this invention, and FIG. 2 is an explanatory diagram showing an example of an apparatus for carrying out the method of this invention. 1... Raw material tank, 2, 5... Conveyor 3...
・-Next mixer 4...Blended raw material hopper 6...Coke powder hopper, 7...Moisture supply pipe, 8...Water injection amount control device, 9...Moisture meter, 10...Air permeability Total, 1
1... Coke powder addition amount calculation device, 12... Setting device, 13... Coke powder cutting control device
Claims (1)
量の水分を添加して混練し、予め定めた通気度に対応す
るコークス等固体燃料添加量の関係から、前記混練配合
原料の実測通気度に応じて所定量のコークス等固体燃料
を添加混合することを特徴とする焼結原料の配合方法。1 Add a predetermined amount of moisture to a sintered blended raw material that does not contain solid fuel such as coke, and knead it, and from the relationship of the amount of solid fuel such as coke added that corresponds to the predetermined air permeability, calculate the actual air permeability of the kneaded blended raw material. A method for blending raw materials for sintering, characterized by adding and mixing a predetermined amount of solid fuel such as coke according to the amount of solid fuel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5478281A JPS5831374B2 (en) | 1981-04-11 | 1981-04-11 | Mixing method of sintering raw materials |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5478281A JPS5831374B2 (en) | 1981-04-11 | 1981-04-11 | Mixing method of sintering raw materials |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57169024A JPS57169024A (en) | 1982-10-18 |
| JPS5831374B2 true JPS5831374B2 (en) | 1983-07-05 |
Family
ID=12980332
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5478281A Expired JPS5831374B2 (en) | 1981-04-11 | 1981-04-11 | Mixing method of sintering raw materials |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5831374B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100380741B1 (en) * | 1998-12-01 | 2003-09-19 | 주식회사 포스코 | Method for granulation of sinter mixture |
| CN109517977A (en) * | 2018-11-26 | 2019-03-26 | 东北大学 | A kind of sintering method of high-chromic vanadium-titanium ferroferrite fine powder with addition of common fine powder of magnetite |
-
1981
- 1981-04-11 JP JP5478281A patent/JPS5831374B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57169024A (en) | 1982-10-18 |
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