Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JPS5854176B2 - Method for preventing particle size segregation of sintered raw fuel - Google Patents
[go: Go Back, main page]

JPS5854176B2 - Method for preventing particle size segregation of sintered raw fuel - Google Patents

Method for preventing particle size segregation of sintered raw fuel

Info

Publication number
JPS5854176B2
JPS5854176B2 JP1967377A JP1967377A JPS5854176B2 JP S5854176 B2 JPS5854176 B2 JP S5854176B2 JP 1967377 A JP1967377 A JP 1967377A JP 1967377 A JP1967377 A JP 1967377A JP S5854176 B2 JPS5854176 B2 JP S5854176B2
Authority
JP
Japan
Prior art keywords
particle size
raw fuel
size segregation
moisture
storage tank
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
Application number
JP1967377A
Other languages
Japanese (ja)
Other versions
JPS53103901A (en
Inventor
博行 吉岡
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.)
Nippon Steel Corp
Original Assignee
Sumitomo Metal Industries 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 Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP1967377A priority Critical patent/JPS5854176B2/en
Publication of JPS53103901A publication Critical patent/JPS53103901A/en
Publication of JPS5854176B2 publication Critical patent/JPS5854176B2/en
Expired legal-status Critical Current

Links

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Description

【発明の詳細な説明】 この発明は焼結機への原料給鉱時における原燃料、つま
り粉コークスの切出し粒度を適正化するための原燃料粒
度偏析防止方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for preventing raw fuel particle size segregation for optimizing the particle size of raw fuel, that is, cut coke breeze, when feeding raw material to a sintering machine.

焼結過程で熱源となる粉コークスの粒度管理は焼結成品
の品質あるいは操業の安定化をはかる上において極めて
重要なこととされている。
Particle size control of coke powder, which is the heat source in the sintering process, is considered to be extremely important in ensuring the quality of sintered products and stabilizing operations.

一般に粉コークスは全原料中に2.5〜4.0優の範囲
で一定配合するが、焼結機への原料給鉱時、貯鉱槽内在
庫量の変動により切出し粒度が周期的に変動することが
知られている。
Generally, coke breeze is mixed in a constant range of 2.5 to 4.0% in all raw materials, but when feeding the raw material to the sintering machine, the cut particle size changes periodically due to fluctuations in the amount of stock in the ore storage tank. It is known to do.

具体的に説明すると、原燃料である粉コークスは、槽内
では第2図Aに示すごとく、槽中央に細粒コークスが、
壁側に粗粒コークスがそれぞれ堆積し、槽内在庫量が多
い場合には細粒コークスが先行して切出され(第2図B
)、在庫減少と共に粗粒コークスが切出される(第2図
C)。
To explain concretely, in the tank, fine coke particles are formed in the center of the tank, as shown in Figure 2A.
Coarse coke is deposited on the wall side, and if there is a large amount of inventory in the tank, fine coke is cut out first (Fig. 2B).
), coarse coke is cut out as the inventory decreases (Figure 2C).

このように、粉コークスを装入した場合槽内での粒度偏
析が著しいため、槽内在庫量の変動毎に周期的な切出し
粒度の変動をきたす。
As described above, when coke breeze is charged, particle size segregation within the tank is significant, and this causes periodic fluctuations in the cut particle size every time the stock amount in the tank changes.

そして、この切出し粒度の変動が原因して、焼結機のウ
ィンドボックス排ガス温度風量の変動をきたし、焼結品
質の劣化を招くという問題を生ずる外、粉コークス粒度
が極端に粗くなった場合、焼結パレットグレード面での
焼付現象を起こし、グレートバーの寿命短縮および漏風
の発生による極端な操業の乱れを余儀なくされるという
憂慮すべき事態が発生する。
This fluctuation in the cut-out particle size causes fluctuations in the wind box exhaust gas temperature and air volume of the sintering machine, causing problems such as deterioration of sintering quality, and if the coke breeze particle size becomes extremely coarse. An alarming situation occurs in which a seizure phenomenon occurs on the surface of the sintered pallet grade, shortening the life of the grate bar and causing extreme operational disruption due to air leakage.

この発明は上記の問題を解消する方法として、粉コーク
スの混合過程における水分の添加量を混合後の含有水分
量に応じて制御することにより、槽内の粒度偏析を軽減
、防止することを特徴とするもので、原燃料切出し粒度
を安定化し得る方法である。
As a method for solving the above problem, this invention is characterized by reducing and preventing particle size segregation in the tank by controlling the amount of water added during the mixing process of coke powder in accordance with the amount of water content after mixing. This is a method that can stabilize the particle size of raw fuel.

この発明は原燃料、つまり粉コークスを混合する過程で
水分を添加する際に、混合された粉コークスの含有水分
の量を検出し、該水分値に基づいてフィードバック操作
により水分を15〜25係の範囲内で添加することによ
り、貯鉱槽内の原燃料粒度偏析を軽減し得る方法である
This invention detects the amount of moisture contained in the mixed coke breeze when adding moisture in the process of mixing raw fuel, that is, coke breeze, and adjusts the moisture content by 15 to 25 by feedback operation based on the moisture value. This is a method that can reduce the particle size segregation of raw fuel in the ore storage tank by adding it within the range of .

第1図はこの発明法を実施するための装置の一例を示す
もので、1は原燃料槽、2は配合ベルトコンベヤー3は
混合装置(破砕機)、4は輸送コンベヤー、5は貯鉱槽
、6は装入コンベヤー、Tは注入装置、8は水分検出器
である。
Figure 1 shows an example of equipment for carrying out the method of the invention, in which 1 is a raw fuel tank, 2 is a blending belt conveyor, 3 is a mixing device (crusher), 4 is a transport conveyor, and 5 is an ore storage tank. , 6 is a charging conveyor, T is an injection device, and 8 is a moisture detector.

即ち、混合した粉コークスを貯鉱槽5へ装入する輸送過
で、混合粉コークスの水分を水分検出器8で検出し、こ
の水分値に基づいてフィードバック操作で注水量を制御
して適正量の水分を添加する。
That is, during transportation of the mixed coke powder to be charged into the ore storage tank 5, the moisture content of the mixed coke powder is detected by the moisture detector 8, and based on this moisture value, the amount of water injected is controlled by feedback operation to ensure an appropriate amount. of water is added.

この方法によれば、貯鉱槽5へ装入する前に当該粉コー
クの含有水分を調整し得るので、貯鉱槽内での粒度偏析
を軽減することができ、切出し粒度の変動を減少させ、
かつ安定化させることが可能である。
According to this method, the water content of the coke breeze can be adjusted before charging it into the ore storage tank 5, so particle size segregation in the ore storage tank can be reduced, and fluctuations in the cut particle size can be reduced. ,
And it is possible to stabilize it.

以下詳細に説明する。This will be explained in detail below.

この発明法は粉コークスの切出し粒度変化が粉コークス
含有水分量に大きく関係するということを実験室的に確
認できたことに基づく、第3図、第4図はその粉コーク
ス切出し粒度変化と水分値の関係を求めた結果を示す図
表で、かかる図表より、水分が少ない場合在庫の粒度変
動による切出し粒度変動が大きく、逆に水分の量が上昇
するにつれて経時的な粒度変動が減少することが認めら
れる。
This invention method is based on the fact that it has been confirmed in the laboratory that the change in the particle size of coke breeze cut out is greatly related to the moisture content of coke breeze. This is a chart showing the results of determining the relationship between the values.The chart shows that when the moisture content is low, the cut-out particle size fluctuations due to stock particle size fluctuations are large, and conversely, as the moisture content increases, the grain size fluctuations over time decrease. Is recognized.

このような現象が起こる理由は、混合過程での水分値と
貯鉱槽内部摩擦係数の関係を示した第5図から明らかで
ある。
The reason why such a phenomenon occurs is clear from FIG. 5, which shows the relationship between the moisture value during the mixing process and the internal friction coefficient of the ore storage tank.

即ち、粉コークスの水分の上昇にともなって槽内粉コー
クス摩擦角が上昇(内部摩擦係数の上昇)し、槽内堆積
時の中央、壁部の粒度偏析が水分が上昇する程少なくな
るためである。
In other words, as the water content of coke breeze rises, the friction angle of the coke breeze in the tank increases (the internal friction coefficient increases), and the particle size segregation at the center and wall during deposition in the tank decreases as the water content rises. be.

なお、摩擦係数μと摩擦角θの関係は、μ=−tanθ
で表わされる。
The relationship between the friction coefficient μ and the friction angle θ is μ=-tanθ
It is expressed as

第6図は第1図に示した装置により実機測定したときの
貯鉱槽内山積み時の粒度偏析状況を示したもので、かか
る図表より、混合過程での水分の添加量が15〜25%
の範囲では槽内粒度偏析が著しく減少することがわかる
Figure 6 shows the particle size segregation situation when piled up in an ore storage tank when measured using the equipment shown in Figure 1. From this diagram, it is clear that the amount of water added during the mixing process is 15 to 25%.
It can be seen that within the range of , the particle size segregation within the tank is significantly reduced.

つまり、これは水分が15〜25饅の範囲では貯鉱槽5
内粉コークスの内部摩擦係数の上昇により、装入時のす
べり(ころがり)が減少し、結果的には第2図Aの状態
で粒度偏析が少なく、第2図B、Cのごとく在庫の減少
の際にも内部摩擦係数が高いためにすべり減少が生じ難
いという理由によるものである。
In other words, this means that when the moisture content is in the range of 15 to 25, the ore storage tank is 5.
Due to the increase in the internal friction coefficient of the internal coke powder, slippage (rolling) during charging is reduced, resulting in less particle size segregation in the state shown in Figure 2 A, and a decrease in inventory as shown in Figure 2 B and C. This is because the coefficient of internal friction is high, so it is difficult to reduce slippage.

一方、水分値が15係以下の場合、前記のごとく経時的
な粒度変動の減少は見られるも、15係以上に比べ水分
が少ないため偏析し易く、又25多以上添加するとコー
クスどうしの付着が生じて棚吊りが発生する。
On the other hand, when the moisture value is less than 15, although a decrease in particle size fluctuation over time can be seen as described above, the moisture content is lower than when the moisture is 15 or more, so segregation is easy to occur, and when more than 25 is added, coke tends to stick to each other. This causes shelf hanging.

従って、在庫の変動による切出し粒度の変動は水分15
〜25%の範囲が適正であるとされる。
Therefore, fluctuations in the cut particle size due to changes in inventory will result in moisture 15
A range of ~25% is considered appropriate.

以上説明したごとく、この発明法によれば、混合粉コー
クスの含有水分を貯鉱槽に入る前の段階で検出し、この
水分値に基づいて混合過程での水分を種々変化させるこ
とにより、貯鉱槽内の粒度偏析の変動を制御することが
できるので、切出し粒度の変動を軽減させることができ
、かつ安定化させ得るものである。
As explained above, according to the method of the present invention, the moisture content of mixed coke powder is detected before it enters the ore storage tank, and the moisture content in the mixing process is varied based on this moisture value. Since fluctuations in grain size segregation within the ore tank can be controlled, fluctuations in cut grain size can be reduced and stabilized.

さらに、この発明法によれば、従来法に比ベグレートバ
ーの寿命は20饅延長でき、ウィンドボックスでの漏風
率は10〜20係減少させ得る。
Further, according to the method of the present invention, the life of the bar can be extended by 20 times compared to the conventional method, and the air leakage rate in the wind box can be reduced by 10 to 20 times.

又、この発明法は簡単な設備改善により既設設備に容易
に適用できる効果がある。
Furthermore, the method of this invention has the advantage that it can be easily applied to existing equipment by simple equipment improvement.

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

第1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、第2図は現状の貯鉱槽内の粉コークス切出し状
況を示す説明図、第8図と第4図は粉コークス切出し粒
度変化と水分値の関係を実験室的に求めた結果を示す図
表、第5図は水分値と内部摩擦角の関係を示す図表、第
6図は第1図の装置により実機測定したときの貯鉱槽内
山積み時の粒度偏析状況を示す図表である。 図中1・・・・・・原燃料槽、2・・・・・・配合ベル
トコンベヤー、3・・・・・・混合装置、4・・・・・
・輸送コンベヤー、5・・・・・・貯鉱槽、6・・・・
・・装入コンベヤー 7・・・・・・注水装置、8・・
・・・・水分検出器。
Fig. 1 is an explanatory diagram showing an example of a device for carrying out the method of this invention, Fig. 2 is an explanatory diagram showing the current state of cutting out coke breeze in an ore storage tank, and Figs. 8 and 4 are illustrations of coke breeze cutting. Figure 5 is a diagram showing the relationship between cut-out particle size change and moisture value obtained in a laboratory. Figure 5 is a diagram showing the relationship between moisture value and internal friction angle. Figure 6 is the result of actual measurement using the equipment shown in Figure 1. This is a chart showing the grain size segregation situation when the ore is piled up in a storage tank. In the diagram, 1... Raw fuel tank, 2... Blending belt conveyor, 3... Mixing device, 4...
・Transportation conveyor, 5...Ore storage tank, 6...
...Charging conveyor 7...Water injection device, 8...
...Moisture detector.

Claims (1)

【特許請求の範囲】[Claims] 1 焼結原燃料混合過程において混合された原燃料の含
有水分を検出し、該水分値に基づいてフィードバック操
作により、上記原燃料の含有水分を15〜25%の範囲
内で添加することにより、貯鉱槽内の原燃料粒度偏析を
軽減し得ることを特徴とする、焼結原燃料の粒度偏析防
止方法。
1. By detecting the moisture content of the raw fuel mixed in the sintering raw fuel mixing process and adding the moisture content of the raw fuel within the range of 15 to 25% by feedback operation based on the moisture value, A method for preventing particle size segregation of sintered raw fuel, characterized by being able to reduce particle size segregation of raw fuel in an ore storage tank.
JP1967377A 1977-02-23 1977-02-23 Method for preventing particle size segregation of sintered raw fuel Expired JPS5854176B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1967377A JPS5854176B2 (en) 1977-02-23 1977-02-23 Method for preventing particle size segregation of sintered raw fuel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1967377A JPS5854176B2 (en) 1977-02-23 1977-02-23 Method for preventing particle size segregation of sintered raw fuel

Publications (2)

Publication Number Publication Date
JPS53103901A JPS53103901A (en) 1978-09-09
JPS5854176B2 true JPS5854176B2 (en) 1983-12-03

Family

ID=12005746

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1967377A Expired JPS5854176B2 (en) 1977-02-23 1977-02-23 Method for preventing particle size segregation of sintered raw fuel

Country Status (1)

Country Link
JP (1) JPS5854176B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20200105693A (en) * 2018-02-28 2020-09-08 토소 화인켐 가부시키가이샤 Composition for forming zinc oxide thin film and method for manufacturing zinc oxide thin film

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02175824A (en) * 1988-12-28 1990-07-09 Nkk Corp Manufacture of sintered ore

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20200105693A (en) * 2018-02-28 2020-09-08 토소 화인켐 가부시키가이샤 Composition for forming zinc oxide thin film and method for manufacturing zinc oxide thin film

Also Published As

Publication number Publication date
JPS53103901A (en) 1978-09-09

Similar Documents

Publication Publication Date Title
RU2635590C2 (en) Method and system to control amount of air of agglomeration car air box
CN113879866B (en) Coal flow conveying method based on traffic flow
BR112013028519B1 (en) cargo loading apparatus for a blast furnace in a coneless loading apparatus and method of loading cargo in a blast furnace using said cargo loading apparatus
JPS5854176B2 (en) Method for preventing particle size segregation of sintered raw fuel
CN116747756A (en) A port-based ore batching method and system
JPS61287615A (en) Automatic control method for belt conveyor equipment
CN104833234B (en) A kind of sintering machine sintering process material bin dynamic equilibrium control method
JP2020094283A (en) Blast furnace operation method
KR100530081B1 (en) A Method for Controlling the Supply of Sinter Cake for Furnace
JP5082556B2 (en) Raw material cutting feeder control method and apparatus
JP2021139037A (en) How to smelt ferronickel
CN106197028A (en) A kind of guarantee expects the speed ratio follow-up control method that position is the most suitable
CN114625096A (en) Dynamic equilibrium control method for material level of sinter mixture ore tank
SU580015A1 (en) Method of automatic control of a screening process
CN110143416A (en) Intelligent sampling device for materials transported by belt conveyor, intelligent sampling control method and system
US4088308A (en) System for controlling the flow of sinter to blast furnace
KR200153473Y1 (en) Raw material charging apparatus for iron ore sintering machine
SU1447861A1 (en) Charge material metering channel
SU1514795A1 (en) METHOD OF LOADING A DOMAIN FURNACE
JPH08127822A (en) Sintering method
TW202528551A (en) Blast furnace operation method
JPH0292990A (en) Method for controlling charging of coal into coke furnace
JPH05287392A (en) Method for supplying raw material in sintering equipment
SU621765A1 (en) Control system for loading charge onto sintering belt
JPH03191030A (en) Production of sintered ore