JPH0774400B2 - Sintered ore manufacturing method - Google Patents
Sintered ore manufacturing methodInfo
- Publication number
- JPH0774400B2 JPH0774400B2 JP2193849A JP19384990A JPH0774400B2 JP H0774400 B2 JPH0774400 B2 JP H0774400B2 JP 2193849 A JP2193849 A JP 2193849A JP 19384990 A JP19384990 A JP 19384990A JP H0774400 B2 JPH0774400 B2 JP H0774400B2
- Authority
- JP
- Japan
- Prior art keywords
- powder
- pallet
- raw material
- coke
- limestone
- 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 - Lifetime
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 62
- 239000000843 powder Substances 0.000 claims description 38
- 235000012255 calcium oxide Nutrition 0.000 claims description 31
- 239000000292 calcium oxide Substances 0.000 claims description 31
- 239000002994 raw material Substances 0.000 claims description 21
- 235000019738 Limestone Nutrition 0.000 claims description 19
- 239000006028 limestone Substances 0.000 claims description 19
- 239000000571 coke Substances 0.000 claims description 16
- 238000011084 recovery Methods 0.000 claims description 15
- 238000005245 sintering Methods 0.000 claims description 8
- 239000010410 layer Substances 0.000 description 17
- 238000000034 method Methods 0.000 description 11
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 5
- 235000011941 Tilia x europaea Nutrition 0.000 description 5
- 239000011230 binding agent Substances 0.000 description 5
- 239000004571 lime Substances 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 238000007796 conventional method Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- LFYJSSARVMHQJB-QIXNEVBVSA-N bakuchiol Chemical compound CC(C)=CCC[C@@](C)(C=C)\C=C\C1=CC=C(O)C=C1 LFYJSSARVMHQJB-QIXNEVBVSA-N 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 238000005065 mining Methods 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 241000287463 Phalacrocorax Species 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
【発明の詳細な説明】 <産業上の利用分野> 本発明は、焼結機パレットの焼結原料層上に石灰石粉を
装入し焼成させ生石灰を得ると共に焼結を行う焼結鉱の
製造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION <Industrial field of application> The present invention is directed to the production of a sintered ore in which limestone powder is charged on a sintering raw material layer of a sinter machine pallet to obtain quick lime by firing and sintering. It is about the method.
<従来の技術> 焼結操業の模式図を第1図に示す。床式ホッパ3からパ
レット1上に切出された床敷鉱の上に給鉱ホッパ4から
切出された原料2を積層して供給する。原料2は点火装
置15で点火されメインブロワ14の通風により原料中の粉
コークスは燃焼し、原料2は焼成され焼結鉱となる。焼
結鉱は粉砕機5で粉砕され、クーラ6で冷却された後、
篩7で分級される。篩上の粒径8〜16mmの成品は床敷鉱
10として床敷ホッパ3に戻され、残余は成品13として高
炉に搬送される。分級された粒径−5mm以下のものは返
鉱11としてミキサ8によって新原料12と混合された後給
鉱ホッパ4に戻される。<Prior Art> A schematic diagram of a sintering operation is shown in FIG. The raw material 2 cut out from the feed hopper 4 is stacked and supplied on the floor bed ore cut out from the floor hopper 3 onto the pallet 1. The raw material 2 is ignited by the igniter 15 and the powder coke in the raw material is burned by the ventilation of the main blower 14, and the raw material 2 is calcined into a sintered ore. After the sinter ore is crushed by the crusher 5 and cooled by the cooler 6,
It is classified by the sieve 7. Products with a particle size of 8 to 16 mm on the sieve are bed mats.
It is returned to the bedding hopper 3 as 10 and the rest is conveyed to the blast furnace as a product 13. The classified particles having a particle size of -5 mm or less are returned to the ore hopper 4 after being mixed with the new raw material 12 by the mixer 8 as the return ore 11.
ところで、一般にパレット上の原料2の通気性を改善す
る手段として、バインダを原料中に混入させることがあ
る。バインダとしては普通生石灰(CaO)がよく用いら
れている。By the way, generally, as a means for improving the air permeability of the raw material 2 on the pallet, a binder may be mixed into the raw material. Commonly used quick lime (CaO) is often used as a binder.
このCaOを安価に製造し利用する方法として、特開昭58
−133331号公報には石灰(CaO)粉9を石灰用ホッパ19
により切出し、原料2の最上部に積層させ点火装置15内
の熱によって石灰粉を生石灰粉(CaO)とし、篩7によ
り返鉱11とともに回収し、バインダとして利用する方法
が提案されている。As a method for inexpensively producing and utilizing this CaO, Japanese Patent Laid-Open No.
-133331 discloses lime (CaO) powder 9 in a lime hopper 19
A method has been proposed in which the lime powder is cut out by the above method, laminated on the uppermost part of the raw material 2, lime powder is converted to quick lime powder (CaO) by the heat in the ignition device 15, and the lime powder is recovered together with the return ore 11 by the sieve 7 and used as a binder.
しかし、この方法では、 (1) 篩7での成品13と返鉱11との分離が完全でな
く、成品13中にバインダが混入する。However, in this method, (1) the separation of the product 13 and the return ore 11 on the sieve 7 is not complete, and the binder is mixed in the product 13.
(2) クーラ6での通風冷却によって、製造されたバ
インダの一部が飛散する。(2) A part of the manufactured binder is scattered by the ventilation cooling by the cooler 6.
等の問題がある。There is a problem such as.
そこで特開平1−147023号公報では、排鉱部近傍のパレ
ット上で、予め焼成された生石灰の比重の大小を利用し
てスクレーバ、ブロワ等により生石灰粉を吸引回収し回
収歩留りを上げる方法が提案されている。Therefore, in Japanese Patent Laid-Open No. 147023/1991, a method is proposed in which on the pallet in the vicinity of the mine ore section, quick lime powder is sucked and collected by a scraper, a blower, etc. by utilizing the magnitude of specific gravity of preliminarily calcined lime to increase the recovery yield. Has been done.
しかし、上記回収方法は、排鉱部近傍での回収なので給
鉱部〜排鉱部間で生石灰粉を上層部に積層したまま鉱石
の焼成が行われ、焼結鉱の生産性を低下させていた。However, since the above recovery method is recovery in the vicinity of the mine ore section, the ore is fired while the quicklime powder is stacked in the upper layer between the mine section and the mine section, which reduces the productivity of the sinter. It was
<発明が解決しようとする課題> 本発明は、焼結機パレット上原料の最上層に粉コークス
と混合した石灰石粉を装入し、点火炉内で加熱着火し生
石灰粉を製造すると共に焼結を行う焼結鉱の製造方法に
おいて、焼結鉱の生産性及びコークス原単位の向上を可
能とする焼結鉱の製造方法を提供することを目的とする
ものである。<Problems to be Solved by the Invention> In the present invention, limestone powder mixed with powder coke is charged in the uppermost layer of a raw material on a sinter machine pallet, and heated and ignited in an ignition furnace to produce quicklime powder and sinter. It is an object of the present invention to provide a method for producing a sinter that enables the productivity of the sinter and the unit of coke to be improved.
<課題を解決するための手段> 本発明は、焼結機パレット上原料の最上層に粉コークス
と混合した石灰石粉を装入し、点火炉内で加熱着火し生
石灰粉を製造すると共に焼結を行う焼結鉱の製造方法に
おいて、該パレット上で生成した生石灰粉の温度を測定
し、生石灰粉の温度が回収設備の耐熱性以下の温度とな
るパレットの位置を見出し、その位置で生成した生石灰
粉をパレット最上層より除去回収することを特徴とする
焼結鉱の製造方法である。<Means for Solving the Problems> In the present invention, limestone powder mixed with powder coke is charged in the uppermost layer of a raw material on a sinter machine pallet, and heated and ignited in an ignition furnace to produce quicklime powder and sinter. In the method for producing a sintered ore, the temperature of the quicklime powder generated on the pallet is measured, the position of the pallet at which the temperature of the quicklime powder is equal to or lower than the heat resistance of the recovery facility is found, and the temperature is generated at that position. It is a method for producing a sinter, characterized in that quicklime powder is removed and recovered from the uppermost layer of the pallet.
<作 用> 本発明を実施するための装置構成の一例を第2図に示
す。<Operation> An example of a device configuration for carrying out the present invention is shown in FIG.
給鉱ホッパ4と点火装置15の間に石灰石用ホッパ19を設
置する。石灰石用ホッパ19に石灰石粉9と粉コークス18
を混合して装入し、石灰石用ホッパ19から原料2の上に
積層して切出す。点火装置15で点火され、粉コークスが
燃焼して石灰石粉が熱分解されて石灰石(CaO)とな
る。A limestone hopper 19 is installed between the mining hopper 4 and the ignition device 15. Limestone hopper 19 and limestone powder 9 and powder coke 18
Are mixed and charged, and the limestone hopper 19 is stacked on the raw material 2 and cut out. It is ignited by the ignition device 15, the coke powder is burned, and the limestone powder is thermally decomposed into limestone (CaO).
点火炉前に台車式の移動式回収フード21を設置する。同
フードの先端に温度計22を取付け、生石灰の上層鵜乃至
下層部の温度を測定し、制御器23を介して移動式回収フ
ード21を目標とする所定の温度の場所までレール24上を
移動させる。すなわち、石灰石粉へのコークス配合比変
更、点火炉の点火熱量の変更時によるパレット上での生
石灰の回収最適点の変化を温度計で生石灰の温度を連続
測定しながら移動式回収フードを最適点へ移動させる仕
組みになっている。なお27はスクレーバ、26は吸引ブロ
ワ、25はホッパである。A trolley-type mobile recovery hood 21 is installed in front of the ignition furnace. A thermometer 22 is attached to the tip of the hood to measure the temperature of the upper and lower cormorants of quicklime, and the movable recovery hood 21 is moved via the controller 23 on the rail 24 to a target predetermined temperature location. Let In other words, the change of the optimum point for collecting quicklime on the pallet due to changes in the coke mixture ratio to limestone powder and changes in the ignition heat of the ignition furnace is used to optimize the mobile recovery hood while continuously measuring the temperature of quicklime with a thermometer. It is a mechanism to move to. 27 is a scraper, 26 is a suction blower, and 25 is a hopper.
回収最適点とは石灰石が生石灰に変成し終わった時点
で、早ければ早い程よいが、通常は粉コークスの燃焼が
完了し、生石灰粉の温度が回収設備の耐熱性以下になっ
た時点を採用すればよい。The optimum recovery point is the time when limestone has been transformed into quick lime, but the earlier the better, but usually, the point when the temperature of the quick lime powder falls below the heat resistance of the recovery facility after the burning of the powder coke is completed. Good.
従って、本発明の方法においては、パレット最上層にお
いて生成した生石灰粉の層が、すみやかに除去されるの
で、生石灰粉層による空気の通過の阻害が最小になり、
従来法である排鉱部直前で回収するのと比較した場合、
原料層の厚みをその分増すことができ、またコークス原
単位の低下が図れる。Therefore, in the method of the present invention, the layer of quicklime powder generated in the uppermost layer of the pallet is promptly removed, so that the inhibition of air passage by the quicklime powder layer is minimized,
When compared with the conventional method of collecting just before the mine section,
The thickness of the raw material layer can be increased correspondingly, and the coke unit consumption can be reduced.
次に実施例に基づいて本発明をより詳細に説明する。Next, the present invention will be described in more detail based on examples.
<実施例> 焼結鉱生産量6700〜6900(dry−t/day)、新原料使用量
(コークス、床敷鉱、返鉱を除く)7200〜7500(dry−t
/day)のDL式焼結機において、生石灰配合率10%(対新
原料)、焼結鉱目標CaO%9.5%の生産前提で、従来方法
(排鉱部直前で回収)と本発明法(生石灰層表面温度10
0℃の位置で回収)の比較を行った。<Example> Sintered ore production 6700-6900 (dry-t / day), new raw material usage (excluding coke, bedding, and return ore) 7200-7500 (dry-t)
/ day) DL type sintering machine, the conventional method (recovery immediately before the mine ore) and the method of the present invention Quicklime layer surface temperature 10
Recovery at 0 ° C.) was performed.
なお石灰石の粉度分布ならびに成分、コークスの粒度分
布は表−1,表−2,表−3に示すとおりである。The particle size distribution of limestone and its components, and the particle size distribution of coke are as shown in Table-1, Table-2 and Table-3.
焼結機パレットの最上層にコークス粉配合率12.5%の石
灰石粉を層厚50mmで装入した。The top layer of the sinter machine pallet was charged with limestone powder with a coke powder content of 12.5% in a layer thickness of 50 mm.
そして点火炉による石灰石表面温度は1100℃に維持し
た。And the surface temperature of limestone by the ignition furnace was maintained at 1100 ℃.
本発明では生石灰を早期回収するため、焼成された生石
灰の吸引回収温度を100℃とした。本実験での生石灰回
収位置は点火炉から4〜6m位置であった。 In the present invention, the quick recovery temperature of the calcined quick lime is set to 100 ° C. in order to quickly recover quick lime. The quick lime recovery position in this experiment was 4 to 6 m from the ignition furnace.
第3図にその結果を示す。The results are shown in FIG.
本発明では従来法に比較し、原料層厚を20mm増やすこと
ができ、またコークス原単位を焼結鉱トン当たり0.7kg
低減できた。In the present invention, compared with the conventional method, the raw material layer thickness can be increased by 20 mm, and the unit of coke is 0.7 kg per ton of sintered ore.
It was possible to reduce.
<発明の効果> 焼結機パレット最上層に粉コークスと石灰石粉を装入
し、点火炉内の熱によって石灰石の焼成を行い、表層の
生石灰粉を吸引回収するプロセスにつき、本発明では生
石灰の温度を測定することにより、パレット上での生石
灰の滞留時間を必要最低時間にして回収したので、回収
後の原料層の通気性が向上し、その分事前に原料の層厚
を厚くしておくことができる。焼結鉱1トン当たりのコ
ークス原単位を減少させることができ、焼結プロセスの
コストを大幅に削減できた。<Effects of the Invention> A process of charging powder coke and limestone powder into the uppermost layer of a sinter machine pallet, firing limestone by heat in an ignition furnace, and sucking and recovering the quicklime powder in the surface layer. By measuring the temperature, the retention time of quicklime on the pallet was set to the minimum required time, and the air permeability of the raw material layer after recovery was improved, and the raw material layer thickness was increased in advance by that amount. be able to. The unit of coke per ton of sintered ore can be reduced, and the cost of the sintering process can be significantly reduced.
【図面の簡単な説明】 第1図は焼結操業の模式図、第2図は本発明を実施する
ための具体的構成の説明図、第3図は本発明と従来法の
焼結原料層厚み及びコークス原単位に及ぼす影響を示す
グラフである。 1……パレット、2……原料、 3……床敷ホッパ、4……給鉱ホッパ、 5……粉砕機、6……クーラ、 7……篩分け、8……ミキサ、 9……石灰石粉+粉コークス、 10……床敷鉱、11……返鉱、 12……新原料、13……製品、 14……ブロワ、15……点火装置、 19……石灰石用ホッパ、20……耐熱ホース、 21……移動式回収フード、22……温度計、 23……制御器、24……レール、 25……ホッパ、26……吸引ブロワ、 27……スクレーバ。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic diagram of a sintering operation, FIG. 2 is an explanatory diagram of a specific structure for carrying out the present invention, and FIG. 3 is a sintering raw material layer of the present invention and a conventional method. It is a graph which shows the influence which it has on thickness and a basic unit of coke. 1 ... Pallet, 2 ... Raw material, 3 ... Bedding hopper, 4 ... Mining hopper, 5 ... Crusher, 6 ... Cooler, 7 ... Sieve, 8 ... Mixer, 9 ... Limestone Powder + powder coke, 10 …… bed ore, 11 …… return ore, 12 …… new raw material, 13 …… product, 14 …… blower, 15 …… igniter, 19 …… limestone hopper, 20 …… Heat-resistant hoses, 21-movable collection hood, 22-thermometer, 23-controller, 24-rail, 25-hopper, 26-suction blower, 27-scraper.
フロントページの続き (72)発明者 安田 素郎 千葉県千葉市川崎町1番地 川崎製鉄株式 会社千葉製鉄所内 (56)参考文献 特開 昭63−247315(JP,A) 特開 平1−147023(JP,A)Front page continuation (72) Inventor Shiro Yasuda No. 1 Kawasaki-cho, Chiba City, Chiba Prefecture Inside the Chiba Works, Kawasaki Steel Co., Ltd. (56) References JP 63-247315 (JP, A) JP 1-147023 ( JP, A)
Claims (1)
スと混合した石灰石粉を装入し、点火炉内で加熱着火し
生石灰粉を製造すると共に焼結を行う焼結鉱の製造方法
において、該パレット上で生成した生石灰粉の温度を測
定し、生石灰粉の温度が回収設備の耐熱性以下の温度と
なるパレットの位置を見出し、その位置で生成した生石
灰粉をパレット最上層より除去回収することを特徴とす
る焼結鉱の製造方法。1. A method for producing a sintered ore in which limestone powder mixed with powder coke is charged in the uppermost layer of a raw material on a sinter machine pallet and heated and ignited in an ignition furnace to produce quick lime powder and sintering. In, the temperature of the quicklime powder generated on the pallet is measured, the position of the pallet at which the temperature of the quicklime powder is lower than the heat resistance of the recovery facility is found, and the quicklime powder generated at that position is removed from the top layer of the pallet. A method for producing a sinter, comprising recovering.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2193849A JPH0774400B2 (en) | 1990-07-24 | 1990-07-24 | Sintered ore manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2193849A JPH0774400B2 (en) | 1990-07-24 | 1990-07-24 | Sintered ore manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0480329A JPH0480329A (en) | 1992-03-13 |
| JPH0774400B2 true JPH0774400B2 (en) | 1995-08-09 |
Family
ID=16314775
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2193849A Expired - Lifetime JPH0774400B2 (en) | 1990-07-24 | 1990-07-24 | Sintered ore manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0774400B2 (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2510193B2 (en) * | 1987-04-03 | 1996-06-26 | 川崎製鉄株式会社 | Sinter production method |
| JPH0639626B2 (en) * | 1987-12-02 | 1994-05-25 | 川崎製鉄株式会社 | Sintered ore manufacturing method |
-
1990
- 1990-07-24 JP JP2193849A patent/JPH0774400B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0480329A (en) | 1992-03-13 |
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