JPS62197B2 - - Google Patents
Info
- Publication number
- JPS62197B2 JPS62197B2 JP7258481A JP7258481A JPS62197B2 JP S62197 B2 JPS62197 B2 JP S62197B2 JP 7258481 A JP7258481 A JP 7258481A JP 7258481 A JP7258481 A JP 7258481A JP S62197 B2 JPS62197 B2 JP S62197B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- less
- coke
- particle size
- 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
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 20
- 239000002245 particle Substances 0.000 claims description 20
- 238000000034 method Methods 0.000 claims description 9
- 238000005096 rolling process Methods 0.000 claims description 4
- 238000009826 distribution Methods 0.000 claims description 3
- 239000010419 fine particle Substances 0.000 claims description 3
- 239000004568 cement Substances 0.000 claims description 2
- 239000011362 coarse particle Substances 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 2
- 239000000571 coke Substances 0.000 description 16
- 238000005245 sintering Methods 0.000 description 12
- 238000005469 granulation Methods 0.000 description 11
- 230000003179 granulation Effects 0.000 description 11
- 239000000446 fuel Substances 0.000 description 9
- 239000000843 powder Substances 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000012256 powdered iron Substances 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 230000035699 permeability Effects 0.000 description 3
- 239000000428 dust Substances 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 238000009628 steelmaking Methods 0.000 description 2
- 239000011398 Portland cement Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
Landscapes
- Solid Fuels And Fuel-Associated Substances (AREA)
- Glanulating (AREA)
Description
〔産業上の利用分野〕
本発明は、例えば冶金用コークスの製造、整粒
過程、さらには輸送過程において、多量に発生す
る粉コークスを転動造粒する方法に関する。
〔従来の技術〕
コークスの製造過程においてコークス炉から排
出された赤熱コークスを消火する場合とか、塊コ
ークスを高炉へ使用するに適した粒度に整粒する
ための破砕時の場合に多くの粉コークスが発生す
る。この他、高炉炉頂よりの排出ガス中にも多く
の粉コークスが含有され、これらはガス灰と称し
捕集されて再利用が図られている。
これら発生粉コークスの利用法の一つとして、
粉鉄鉱石の焼結用燃料として活用することのでき
る粉コークスの造粒方法が特開昭54−127902号公
報、特開昭54−129003号公報に開示されている。
〔発明が解決しようとする問題点〕
粉鉄鉱石の焼結用燃料として造粒コークスに必
要な性状として、焼結に際しての通気性を維持で
きる粒径であること、焼結機への装入過程で粉化
しない適度の強度を有することが要求される。
他方、鉄鋼製造工程で捕集される製鋼ダスト等
の含鉄粉塵を返り鉱として焼結原料とするための
造粒も行われているが、上記粉コークスはその表
面状態が尖鋭突起の集合状態にあり、また多数の
気孔を有しており、返り鉱の場合とはその性状及
び形状を全く異にし、これら含鉄粉塵の造粒方法
をそのまま適用して効率よく造粒することは極め
て困難である。
本発明の目的は、とくに粉鉄鉱石の焼結用燃料
として上記条件を満たし得る造粒コークスを得る
ための粉コークスを効率良く造粒する方法を提供
することにある。
〔問題点を解決するための手段〕
本発明は、かかる粉コークスを造粒する場合、
粒径が0.5〜0.15mm範囲の中間粒部分が多く存在
すると造粒性が著しく阻害されるという知見に基
いて完成したものである。この中間粒がドラム
型、あるいはデイスク型の転動造粒装置による造
粒において、造粒性を阻害する要因については、
未だ理論的解明に至つてはいないが、この中間粒
部分は自身粒形成の核となり難く、また付着粒子
としても作用し難いためと考えられる。
従つて、効率的な造粒を得るためには造粒性を
阻害する中間粒は予め篩分け除去するか粉砕して
一定の含有量以下に調整しておくことが必要で、
本発明においては上記0.5〜0.15mm範囲の中間粒
部分は、原料粉コークス中40重量%以下、好まし
くは30重量%以下になるように調整する。
すなわち本発明は、粒径分布を調整して粒径
0.5〜0.15mmの中間粒が40重量%以下、0.15mm未満
の微粒が20〜50重量%、且つ0.5mmを超え1mm以
下の粗粒が80重量%未満である粒径が1mm以下の
原料粉コークスを調製し、該原料粉コークス100
重量部に3〜10重量部のセメントを配合し、さら
に最終的に水分が12〜20重量%になるように水分
を添加調整したのち転動造粒することによつて、
特に粉鉄鉱石の焼結用燃料に好適に利用できる造
粒粉コークスを得るものである。
本発明において使用される粉コークスは、たと
えばコークス製造における消火塔沈澱池から回収
される粉コークス、あるいは乾式消火における排
気中から回収される粉コークス等のうち、第1表
に例示するような粒度構成を有する粒径が1mm以
下の水分1重量%以下または乾燥状態とした微細
粉コークスである。
[Industrial Field of Application] The present invention relates to a method for rolling granulating coke powder, which is generated in large quantities during, for example, the production of metallurgical coke, the sizing process, and the transportation process. [Prior art] In the coke manufacturing process, many coke breezes are used when extinguishing red-hot coke discharged from a coke oven, or when crushing lump coke to size it to a size suitable for use in a blast furnace. occurs. In addition, the exhaust gas from the top of the blast furnace also contains a large amount of coke breeze, which is called gas ash and is collected for reuse. One of the ways to use the generated coke powder is to
A method for granulating coke powder that can be used as a fuel for sintering powdered iron ore is disclosed in JP-A-54-127902 and JP-A-54-129003. [Problems to be solved by the invention] The properties required for granulated coke as a fuel for sintering powdered iron ore include a particle size that can maintain air permeability during sintering, and a requirement for charging into a sintering machine. It is required to have appropriate strength so that it does not turn into powder during the process. On the other hand, granulation is also carried out to use iron-containing dust such as steelmaking dust collected in the steelmaking process as return ore and use it as a sintering raw material, but the surface condition of the coke powder is a collection of sharp protrusions. It also has many pores, and its properties and shape are completely different from those of return ore, and it is extremely difficult to granulate it efficiently by applying the granulation method of these iron-containing dusts as is. . An object of the present invention is to provide a method for efficiently granulating coke powder in order to obtain granulated coke that can satisfy the above conditions, particularly as a fuel for sintering powdered iron ore. [Means for Solving the Problems] The present invention provides that when granulating such coke powder,
This was completed based on the knowledge that granulation performance is significantly inhibited when a large amount of intermediate particles with particle diameters in the range of 0.5 to 0.15 mm are present. Regarding the factors that inhibit the granulation of intermediate grains when granulated using a drum-type or disk-type rolling granulator,
Although it has not yet been theoretically elucidated, it is thought that this intermediate grain portion is difficult to become a nucleus for the formation of its own grains, and is also difficult to act as attached particles. Therefore, in order to obtain efficient granulation, it is necessary to remove intermediate grains that inhibit granulation properties by sieving or pulverizing them to keep the content below a certain level.
In the present invention, the intermediate grain portion in the range of 0.5 to 0.15 mm is adjusted to be 40% by weight or less, preferably 30% by weight or less in the raw coke powder. In other words, the present invention adjusts the particle size distribution to increase the particle size.
Raw material powder with a particle size of 1 mm or less, with 40% by weight or less of intermediate particles of 0.5 to 0.15 mm, 20 to 50 weight% of fine particles of less than 0.15 mm, and less than 80 weight% of coarse particles of more than 0.5 mm and 1 mm or less. Prepare coke, 100% of the raw coke powder
By blending 3 to 10 parts by weight of cement to the parts by weight, further adding and adjusting moisture so that the final moisture content is 12 to 20% by weight, and then rolling granulation.
Particularly, granulated coke powder can be obtained which can be suitably used as a fuel for sintering powdered iron ore. The coke powder used in the present invention is, for example, coke powder recovered from a fire extinguishing tower sedimentation basin in coke manufacturing, or coke powder recovered from exhaust gas in dry extinguishing, and has a particle size as illustrated in Table 1. This is fine powder coke with a particle size of 1 mm or less and a moisture content of 1% by weight or less or in a dry state.
コークス製造装置の湿式消火塔に付属した沈澱
池から回収した粉コークスを第2表に示す粒度構
成に調整した原料粉コークス100重量部に対し、
普通ポルトランドセメント6重量部配合し、全量
として40Kgを混練機によつて撹拌、混合して原料
粉コークス中に一様に分散させたのち、デイスク
型造粒機(パンペレタイザー:パン直径0.6m、
パン探さ0.12m)を用いて、パン傾斜角55度、回
転数12rpmとして、配合原料を一定量ずつ連続的
に25分間にわたつて供給し、この間水を連続的に
供給して、最終的に水分含有量が16重量%となる
ように調湿して造粒した。これによつて、焼結用
燃料として利用できる粒径0.5mm以上の造粒コー
クスを得た。
第2表におけるNo.1〜4は本発明の例を示し、
No.5〜8は比較例を示す。同表の判定欄におい
て、原料粉コークスの粒度分布で焼結用燃料とし
て通気性を阻害する粒径0.5mm未満の微粉の割合
を以て造粒効率とした。具体的には同表の原料粉
コークス粒度において0.5mm以下の微粒の割合の
造粒後の減少の比率によつて、70重量%以上の場
合を良(◎)とし、また60重量%以上70重量%未
満をやや不良(△)とし、更に、それ未満を不良
(×)とした。
同表を参照して、本発明の造粒法によつて原料
粉コークスの中の微粉の大部分を造粒焼結用燃料
として利用できたことが判る。しかも本発明によ
つて得た造粒コークスは粉化の問題もなく、焼結
用燃料として耐え得る充分な強度を有するもので
あつた。
For 100 parts by weight of raw coke powder collected from the sedimentation tank attached to the wet fire extinguishing tower of a coke manufacturing equipment and adjusted to the particle size composition shown in Table 2,
6 parts by weight of ordinary Portland cement was blended, and a total of 40 kg was stirred and mixed using a kneader to uniformly disperse it in the raw coke powder.
Using a pan with a pan angle of 0.12 m and a pan inclination angle of 55 degrees and a rotation speed of 12 rpm, the blended raw materials were continuously supplied in a fixed amount for 25 minutes, during which time water was continuously supplied, and finally The moisture content was adjusted to 16% by weight and granulated. As a result, granulated coke with a particle size of 0.5 mm or more, which can be used as a sintering fuel, was obtained. Nos. 1 to 4 in Table 2 indicate examples of the present invention,
Nos. 5 to 8 show comparative examples. In the evaluation column of the same table, the granulation efficiency was defined as the proportion of fine powder with a particle size of less than 0.5 mm that inhibits air permeability as a sintering fuel in the particle size distribution of raw coke powder. Specifically, based on the reduction ratio of the proportion of fine particles of 0.5 mm or less in the raw material coke particle size in the same table after granulation, 70% by weight or more is considered good (◎), and 60% by weight or more is 70% by weight. If it was less than % by weight, it was rated as slightly poor (△), and if it was less than that, it was rated as poor (x). Referring to the same table, it can be seen that by the granulation method of the present invention, most of the fine powder in the raw coke powder could be used as fuel for granulation and sintering. Moreover, the granulated coke obtained by the present invention had no problem of pulverization and had sufficient strength to withstand as a sintering fuel.
本発明によつて、粉コークスを効率よく転動造
粒することができ、しかも得られた造粒物は鉱石
の焼結用燃料に適した通気性と強度を具備したも
のである。
According to the present invention, coke powder can be efficiently rolled and granulated, and the resulting granules have air permeability and strength suitable as a fuel for sintering ores.
Claims (1)
粒が40重量%以下、0.15mm未満の微粒が20〜50重
量%、且つ0.5mmを超え1mm以下の粗粒が80重量
%未満である粒径が1mm以下の原料粉コークスを
調製し、該原料粉コークス100重量部に3〜10重
量部のセメントを配合し、さらに最終的に水分が
12〜20重量%になるように水分を添加調整したの
ち転動造粒することを特徴とする粉コークスの造
粒方法。1 Adjust the particle size distribution so that intermediate particles with a particle size of 0.5 to 0.15 mm are 40% by weight or less, fine particles of less than 0.15 mm are 20 to 50% by weight, and coarse particles with a particle size of more than 0.5 mm and 1 mm or less are less than 80% by weight. Prepare raw coke powder with a particle size of 1 mm or less, add 3 to 10 parts by weight of cement to 100 parts by weight of the raw coke powder, and finally remove moisture.
A method for granulating coke powder, which comprises adding and adjusting water content to 12 to 20% by weight and then granulating it by rolling.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7258481A JPS57187391A (en) | 1981-05-13 | 1981-05-13 | Powder coke granulation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7258481A JPS57187391A (en) | 1981-05-13 | 1981-05-13 | Powder coke granulation |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57187391A JPS57187391A (en) | 1982-11-18 |
| JPS62197B2 true JPS62197B2 (en) | 1987-01-06 |
Family
ID=13493567
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7258481A Granted JPS57187391A (en) | 1981-05-13 | 1981-05-13 | Powder coke granulation |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57187391A (en) |
-
1981
- 1981-05-13 JP JP7258481A patent/JPS57187391A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57187391A (en) | 1982-11-18 |
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