JPH03183732A - Manufacture of quicklime by sintering machine - Google Patents
Manufacture of quicklime by sintering machineInfo
- Publication number
- JPH03183732A JPH03183732A JP32258989A JP32258989A JPH03183732A JP H03183732 A JPH03183732 A JP H03183732A JP 32258989 A JP32258989 A JP 32258989A JP 32258989 A JP32258989 A JP 32258989A JP H03183732 A JPH03183732 A JP H03183732A
- Authority
- JP
- Japan
- Prior art keywords
- limestone
- powder
- sintering machine
- layer
- particle size
- 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
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 title claims abstract description 32
- 238000005245 sintering Methods 0.000 title claims abstract description 25
- 239000000292 calcium oxide Substances 0.000 title claims abstract description 16
- 235000012255 calcium oxide Nutrition 0.000 title claims abstract description 16
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- 235000019738 Limestone Nutrition 0.000 claims abstract description 31
- 239000006028 limestone Substances 0.000 claims abstract description 31
- 239000000843 powder Substances 0.000 claims abstract description 18
- 239000002245 particle Substances 0.000 claims abstract description 12
- 239000000203 mixture Substances 0.000 claims abstract description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 7
- 239000000571 coke Substances 0.000 abstract description 3
- 239000002994 raw material Substances 0.000 description 13
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 235000010216 calcium carbonate Nutrition 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000010494 dissociation reaction Methods 0.000 description 1
- 230000005593 dissociations Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000005204 segregation Methods 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 238000004448 titration Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
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〉
本発明は、ドワイトロイド式焼結機を用いた高炉用原料
の焼結工程において、焼結機パレットの最上層で生石灰
を製造する方法に係わり、生石灰の品質及び生産性を向
上する方法に関するものである。[Detailed Description of the Invention] <Industrial Application Field> The present invention relates to a method for producing quicklime in the uppermost layer of a sintering machine pallet in a sintering process of raw material for a blast furnace using a Dwight Lloyd sintering machine. The present invention relates to a method for improving the quality and productivity of quicklime.
〈従来の技術〉
ドワイトロイド式焼結機を用いた高炉用原料の焼結操業
の模式図を第2図に示す、床敷鉱用ホッパー3からバレ
ン)1上に切出された床敷鉱の上に給鉱ホツパ−4から
切出された焼結原料2を積層して供給する。原料2は点
火装置f15で点火されメインブロワ−14の通風によ
り焼結原料中の粉コークスは燃焼し、焼結原料は焼成さ
れて焼結鉱となる。焼結鉱は粉砕415で粉砕され、ク
ーラー6で冷却された後、篩分け117で分級される。<Prior art> Figure 2 shows a schematic diagram of a sintering operation for blast furnace raw materials using a Dwight Lloyd sintering machine. The sintering raw material 2 cut out from the feed hopper 4 is stacked and supplied on top of the sintered material 2. The raw material 2 is ignited by the igniter f15, and the coke powder in the sintering raw material is combusted by ventilation from the main blower 14, and the sintering raw material is fired to become sintered ore. The sintered ore is crushed in a crusher 415, cooled in a cooler 6, and then classified in a sieve 117.
そして篩上の粒径8〜16mの成品は床敷鉱lOとして
床敷ホッパー3に戻され、残余は成品13として高炉に
輸送される。一方分級された粒径−5am以下のものは
返しtlE 11としてミキサー8によって新原料12
と混合された後給鉱ホツパ−4に戻される。The product on the sieve with a particle size of 8 to 16 m is returned to the bedding hopper 3 as bedding ore 1O, and the remainder is transported to the blast furnace as product 13. On the other hand, the classified particles with a particle size of -5 am or less are returned to the mixer 8 as tlE 11 and are then transferred to the new raw material 12.
After being mixed with ore, it is returned to the feed hopper 4.
さて、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、バインダーを原料中に混合することがあり、
バインダーとしては普通生石灰(CaO〉がよく用いら
れている。Generally, as a means to improve the air permeability of the raw material 2 on the pallet, a binder may be mixed into the raw material.
Quicklime (CaO) is commonly used as a binder.
このCaOを安価に製造する方法として、特開昭58−
133331号公報には石灰(CaCOs)粉9を石灰
用ホッパー19から切り出し、原料2の最」二部に積層
さ・し点火装置15内の熱によって下記(1)式の反応
を行わせ、
CaCO3→CaO+ Cog+ΔH−−−−−〜−−
−(1)(ΔH:エンタルピー差)
石灰石粉から生石灰粉を製造する方法が提案されている
。As a method for producing this CaO at low cost, JP-A-58-
Publication No. 133331 discloses that lime (CaCOs) powder 9 is cut out from a lime hopper 19, layered on the bottommost part of the raw material 2, and caused to undergo a reaction according to the following formula (1) with the heat in the igniter 15, to form CaCO3. →CaO+ Cog+ΔH−−−−−−−
-(1) (ΔH: enthalpy difference) A method for producing quicklime powder from limestone powder has been proposed.
しかし、COlの解離は石灰石の表面から内部へ徐々に
進行していくので、粒度範囲の広い石灰石を焼成すると
きに、小さい粒度に焼成の照準を合わせれば大きい粒度
は未焼成が多く、大きい粒度に照tBを合わせれば小さ
い粒度は過坑底となり、生産効率上また品質上問題があ
った。However, the dissociation of COl progresses gradually from the surface to the inside of limestone, so when firing limestone with a wide range of grain sizes, if you aim for firing at small grain sizes, the larger grains are often unfired, and the larger grains If tB is combined with tB, the small particle size will result in over-bottoming, which poses problems in terms of production efficiency and quality.
〈発明が解決しようとする課題〉
本発明の目的は、焼結工程を利用した生石灰の製造方法
において、従来より高効率で、かつ高品質の生石灰を製
造する方法を提供することにある。<Problems to be Solved by the Invention> An object of the present invention is to provide a method for producing quicklime using a sintering process with higher efficiency and higher quality than before.
〈課題を解決するための手段〉
すなわち、本発明は、ドワイトロイド式焼結機を用いた
焼結工程において、焼結機パレットの最上層に石灰石粉
と粉コークスの混合物を装入して点火炉内の熱によって
石灰石粉から生石灰粉を生成する際に、石灰石層の高さ
方向の粒度分布をドラムシェードにより上は粗く下は細
かく装入することを特徴とする焼結機での生石灰の製造
方法である。<Means for Solving the Problems> In other words, the present invention provides a sintering process using a Dwight Lloyd sintering machine, in which a mixture of limestone powder and coke powder is charged into the top layer of a sintering machine pallet. When producing quicklime powder from limestone powder using heat in a furnace, the particle size distribution in the height direction of the limestone layer is controlled by a drum shade, which is used to charge coarse limestone at the top and finely at the bottom. This is the manufacturing method.
く作 用〉
本発明では、焼結機パレット上の最上層にコークス粉と
石灰石粉を装入する際、ドラムシェードにより石灰石層
の高さ方向において、粒度偏析を起こし、上層部から下
層部において粒径が低下していくように装入したので、
粗粒石灰石を最も熱が多い9m域、細粒石灰石を最も熱
が少ない領域に装入することができ、その結果、石灰石
の未焼成と過坑底を大幅に減少できる。Effect> In the present invention, when charging coke powder and limestone powder to the uppermost layer on the sintering machine pallet, particle size segregation occurs in the height direction of the limestone layer by the drum shade, and the particles are separated from the upper layer to the lower layer. Since it was charged so that the particle size decreased,
Coarse-grained limestone can be charged in the 9m area where the most heat is generated, and fine-grained limestone can be charged in the area with the least amount of heat, and as a result, uncalcined limestone and excessive bottom of the mine can be significantly reduced.
上記装入を行うための具体的構成を第1図に示す0石灰
石用ホッパー19のドラムフィーダー20によりコーク
スわ)と石灰石粉との混合物9の切り出しを行い、これ
をドラムシェード21に落下させる。A concrete configuration for performing the above charging is shown in FIG. 1. A mixture 9 of coke and limestone powder is cut out by a drum feeder 20 of a hopper 19 for limestone, and is dropped into a drum shade 21.
粉コークス及び石灰石粉は回転するドラムシューにて乳
化し4N塩酸による中和滴定を1テい5分後の4N塩酸
使用量(d)である。The coke powder and limestone powder were emulsified in a rotating drum shoe and subjected to neutralization titration with 4N hydrochloric acid for 1 hour.The amount of 4N hydrochloric acid used after 5 minutes was (d).
〈発明の効果〉
焼結機パレットの最上層に粉コークスと石灰石粉を装入
して坑底を行い、点火炉内の熱によって石灰石粉から生
石灰粉を生成するプロセスにおいて、石灰石層の高さ方
向の石灰石の粒度分布をドラムシェードによってffi
’J m シたので、生石灰の生産性及び品質を向上で
きた。<Effects of the invention> In the process of charging coke powder and limestone powder to the top layer of the sintering machine pallet to form the bottom of the pit, and generating quicklime powder from the limestone powder using heat in the ignition furnace, the height of the limestone layer was reduced. Grain size distribution of limestone in direction ffi by drum shade
'J m was able to improve the productivity and quality of quicklime.
従って、従来方式と比較した場合、生石灰の製造におい
て大幅なコスト削減が可能となった。Therefore, when compared with the conventional method, it has become possible to significantly reduce costs in producing quicklime.
第1図は本発明を実施するための装置の説明図、第2図
は焼結操業工程の説明図である。
l・・・パレット、
3・・・床敷鉱用ホッパー
4・・・焼結原料給鉱ホッパー
5・・・粉砕機、
7・・・篩分は機、
2・・・焼結原料、
6・・・クーラー
8・・・ミキサー
9・・・石灰石粉と粉コークスとの混合物、lO・・・
床敷鉱、 11・・・返し鉱、12・・・新
原料、 13・・・製 品、14・・・ブロ
ワ、 15・・・点火装置、19・・・石灰
石用ホッパー
20・・・ドラムフィーダー 21・・・ドラムシェ
ード。FIG. 1 is an explanatory diagram of an apparatus for implementing the present invention, and FIG. 2 is an explanatory diagram of a sintering operation process. l...Pallet, 3...Hopper for bedding ore 4...Sintering raw material feeding hopper 5...Crusher, 7...Sieving machine, 2...Sintering raw material, 6 ...Cooler 8...Mixer 9...Mixture of limestone powder and coke powder, lO...
Bed ore, 11... Return ore, 12... New raw material, 13... Product, 14... Blower, 15... Ignition device, 19... Limestone hopper 20... Drum Feeder 21...Drum shade.
Claims (1)
焼結機パレットの最上層に石灰石粉と粉コークスの混合
物を装入して点火炉内の熱によって石灰石粉から生石灰
粉を生成する際に、石灰石層の高さ方向の粒度分布をド
ラムシェードにより上は粗く下は細かく装入することを
特徴とする焼結機での生石灰の製造方法。In the sintering process using a Dwight Lloyd sintering machine,
When charging a mixture of limestone powder and coke powder to the top layer of the sintering machine pallet and generating quicklime powder from the limestone powder using the heat in the ignition furnace, the particle size distribution in the height direction of the limestone layer is measured using a drum shade. A method for producing quicklime using a sintering machine, which is characterized by charging coarsely at the top and finely at the bottom.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP32258989A JPH03183732A (en) | 1989-12-14 | 1989-12-14 | Manufacture of quicklime by sintering machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP32258989A JPH03183732A (en) | 1989-12-14 | 1989-12-14 | Manufacture of quicklime by sintering machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03183732A true JPH03183732A (en) | 1991-08-09 |
Family
ID=18145388
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP32258989A Pending JPH03183732A (en) | 1989-12-14 | 1989-12-14 | Manufacture of quicklime by sintering machine |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03183732A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105907952A (en) * | 2016-07-04 | 2016-08-31 | 湖南华菱湘潭钢铁有限公司 | Method of phenol hydrogen sludge participating in sintering ore blending |
-
1989
- 1989-12-14 JP JP32258989A patent/JPH03183732A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105907952A (en) * | 2016-07-04 | 2016-08-31 | 湖南华菱湘潭钢铁有限公司 | Method of phenol hydrogen sludge participating in sintering ore blending |
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