JPS6069192A - Preparation of coke for metallurgy - Google Patents
Preparation of coke for metallurgyInfo
- Publication number
- JPS6069192A JPS6069192A JP17773683A JP17773683A JPS6069192A JP S6069192 A JPS6069192 A JP S6069192A JP 17773683 A JP17773683 A JP 17773683A JP 17773683 A JP17773683 A JP 17773683A JP S6069192 A JPS6069192 A JP S6069192A
- Authority
- JP
- Japan
- Prior art keywords
- coke
- particle size
- added
- amt
- dust
- 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
Landscapes
- Coke Industry (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は冶金用コークスの製造法に関し、さらに詳しく
は、高炉等に使用するコークスの粒度を原料石炭に微粉
コークスを添加して工夫を凝らすことにより製品コーク
ス粒度を制御する冶金用コークスの製造法に関する。[Detailed Description of the Invention] The present invention relates to a method for producing metallurgical coke, and more specifically, the particle size of product coke is controlled by adding pulverized coke to coking coal to control the particle size of coke used in blast furnaces, etc. This invention relates to a method for producing metallurgical coke.
一般に高炉等の冶金炉においては燃料或いは還元剤とし
てコークスが使用されているが、このコークスの品質は
、灰分、PlSの量が少ないことと、炉床に達するまで
粉砕されずに通風を助けるために耐圧力(強度)の高い
こと等により評価されしかして、コークスの灰分、P、
Sについては原料炭を選択することにより比較的容易に
制御することが可能であるが、コークスの強度について
、これを制御するには複雑な配合技術や高炉の操業技術
が要求される。Coke is generally used as a fuel or reducing agent in metallurgical furnaces such as blast furnaces, but the quality of this coke is due to its low ash and PLS content, and because it is not crushed until it reaches the hearth, which helps ventilation. The ash content of coke, P,
S can be controlled relatively easily by selecting the coking coal, but controlling coke strength requires complex blending technology and blast furnace operation technology.
そして、コークスの強度は高炉における通気性を維持す
る上で重要であり、通常、ドラム強度(30回転後の刊
5mn+指数:D■1530.150回転後の+15昧
指数:D I +5150)、タンブラ−強度、CO2
によるガス化反応後のコークスの回転強度(反応後強度
)等で測定される。The strength of coke is important in maintaining air permeability in the blast furnace, and usually the drum strength (5 mn + index after 30 revolutions: D 1530. +15 mn index after 150 revolutions: D I +5150), tumbler strength -Intensity, CO2
It is measured by the rotational strength of coke after the gasification reaction (strength after reaction).
さらに、高炉での通気性に関わるものとしてコークス粒
度も重要な評価要素の−っであり、コークスの粒度につ
いては高炉装入前のコークスを篩分析し、調和平均粒径
として、或いは、ドラム強度試験後の+50關指数(I
) I 5.3°)としてめられる。 また、コークス
強度が低下したような場合、コークス粒度を上げること
によって強度低下をカバーする方法が採用されることが
あるが、このためには篩目を天外<シて平均粒径を上げ
るが、コークス塊の歩留が低下する。一方、コークス粒
度は製造時における制御は難かしく、乾留後の置時間の
調整等乾留条件を変更するか、特殊な配合条件にするし
か方法がなく、実際」二制御することは不可能であった
。Furthermore, coke particle size is an important evaluation factor as it relates to air permeability in the blast furnace.The coke particle size is determined by sieve analysis of the coke before charging into the blast furnace, and the harmonic average particle size or drum strength. +50 index after the test (I
) I 5.3°). In addition, in cases where the coke strength has decreased, a method is sometimes adopted to compensate for the decrease in strength by increasing the coke particle size. The yield of coke lumps decreases. On the other hand, it is difficult to control the coke particle size during production, and the only way to do so is to change the carbonization conditions, such as adjusting the standing time after carbonization, or to use special blending conditions.In reality, it is impossible to control coke particle size. Ta.
本発明は上記に説明したような、技術的背景および問題
点に鑑み、種々の実験、検討を重ねた結果、原料配合段
階で石炭原料に小量の微粉コークスを配合し、この微粉
コークスの添加量を調整することによって比較的容易に
製品コークスの粒度が制御できる知見を得て完成された
新規なコークス粒度の制御ができる冶金用コークスの製
造法を提供するものである。In view of the technical background and problems as explained above, and as a result of various experiments and studies, the present invention has been developed by blending a small amount of fine coke with the coal raw material at the raw material blending stage, and by adding this fine coke. The object of the present invention is to provide a novel method for producing metallurgical coke that allows the particle size of coke to be controlled, which has been completed based on the knowledge that the particle size of product coke can be controlled relatively easily by adjusting the amount.
本発明に係る冶金用コークスの製造法の特徴とするとこ
ろは、冶金用コークスの製造に際して、原料石炭に微粉
コークスを添加すると共に、目的とする製品粒度に応じ
て該微粉コークスの添加量を調整することによって製品
コークスの粒度を制御することにある。The feature of the method for producing metallurgical coke according to the present invention is that when producing metallurgical coke, fine coke is added to raw coal, and the amount of the fine coke added is adjusted according to the target product particle size. The purpose is to control the particle size of the coke product.
本発明に係る冶金用コークスの製造法について詳細に説
明する。The method for producing metallurgical coke according to the present invention will be explained in detail.
即ち、第1図は原料石炭に一100メツシュ(−0,1
5mm)に粉砕した微粉コークスを0〜10%の範囲で
添加し、これを乾留して得られたコークスの粒度と微粉
コークス添加量の関係を示したものであり、コークス粒
度はこの第1図から明らかなように、微粉コークスの添
加量によって大きく影響を受けることがわかり、特に、
微粉コークスの添加量が7.5%までは両者に正の一次
相関が認められる。例えば、この場合具体的には微粉コ
ークスの添加量を1%増加させると製品コークスの平均
粒度を0.9mb+向上させることがで外る。また、1
0%の添加量かられかるように金粉コークスの添加量を
8%を越えて増加させても製品コークスの粒度を制御す
る効果はそれ以上期待できない。従って、製品コークス
の目標粒度が設定されれば、第1図における相関から原
料石炭に添加する微粉コークスの量が決まることになり
、微粉コークスの添加量を調整するだけで比較的広範囲
に亘り、製3−
品コークスの粒度を容易に制御することかで外るのであ
る。That is, Fig. 1 shows that 1100 mesh (-0,1
Figure 1 shows the relationship between the particle size of the coke obtained by adding 0 to 10% of fine coke crushed to 5 mm) and carbonizing it and the amount of fine coke added. As is clear from the above, it is found that the amount of fine coke added has a large effect, and in particular,
A positive linear correlation is observed between the two when the amount of fine coke added is up to 7.5%. For example, in this case, if the amount of fine coke added is increased by 1%, the average particle size of the coke product can be improved by 0.9 mb+. Also, 1
Even if the amount of gold powder coke added exceeds 8%, as seen from the amount of 0% added, no further effect of controlling the particle size of the product coke can be expected. Therefore, once the target particle size of the product coke is set, the amount of fine coke to be added to the raw coal can be determined from the correlation shown in Figure 1, and by simply adjusting the amount of fine coke to be added, it can be applied over a relatively wide range. This can be achieved by easily controlling the particle size of the manufactured coke.
さらに、この微粉コークスの添加量については基本的に
、製品コークスの目標粒度に合わせて調節されるわけで
あるが、しかし、当然ながら粒度条件は満足しても冶金
用コークスとして要求される他の品質が確保されていな
ければ、事実上使用が困難となる。そこで、本発明者は
コークスの品質として特に重要な強度との関係について
も調査してみた。即ち、第2図はやはり原料石炭に一1
00メツシュ(−0,15mm)に粉砕された微粉コー
クスを0〜10%の範囲で添加し、これを乾留して得ら
れた製品コークスのドラム強度CD I+5”)の値を
測定した結果であるが、微粉コークス添加量が5%まで
はベース(微粉コークス=θ%)と同等以上の強度を示
しており、この5%を越える添加量では強度が低下する
傾向が認められ、従って、製品コークス粒度を調整する
ために必要な微粉コークス量は原料石炭に対して5%以
下に保持するのが望ましいといえる。Furthermore, the amount of fine coke added is basically adjusted according to the target particle size of the product coke, but of course, even if the particle size condition is satisfied, there are other factors required for metallurgical coke. If quality is not ensured, it will be practically difficult to use. Therefore, the present inventor also investigated the relationship between coke quality and strength, which is particularly important. In other words, Figure 2 shows that raw coal has a
These are the results of measuring the drum strength (CD I+5") of the product coke obtained by adding fine coke powder crushed to 0.00 mesh (-0.15 mm) in the range of 0 to 10% and carbonizing it. However, when the amount of fine coke added is up to 5%, it shows a strength equal to or higher than that of the base (fine coke = θ%), and when the amount exceeds 5%, the strength tends to decrease, and therefore the product coke It can be said that it is desirable to keep the amount of fine coke required to adjust the particle size to 5% or less based on raw coal.
4一
本発明に係る冶金用コークスの製造法について実施例を
説明する。41 Examples of the method for producing metallurgical coke according to the present invention will be described.
実施例
第1表に示すような、原料石炭(粉炭および成型炭)と
微粉コークス(−100メツシユ)を添加しない場合と
添加した場合の配合(第2表)により乾留温度1250
〜1280℃で高炉用コークスを製造した。Examples As shown in Table 1, the carbonization temperature was 1250 depending on the formulation (Table 2) with and without the addition of raw coal (pulverized coal and briquette coal) and pulverized coke (-100 mesh).
Blast furnace coke was produced at ~1280°C.
なお、実施例No、2、No、3、No、5およびNo
。In addition, Example No. 2, No. 3, No. 5, and No.
.
6(本発明)における目標粒度は夫々42mm、42.
5mm、40.5mmおよび42.5+nmとして設定
した。この結果は第2表に示すように略目標通りの粒度
を有する製品コークスを得ることができ、また、従来法
と比して大粒径で、かつ、強度についても同等またはそ
れ以上の品質を備えていることがわかる。The target particle sizes for 6 (invention) are 42 mm and 42 mm, respectively.
5mm, 40.5mm and 42.5+nm. As shown in Table 2, this result shows that it is possible to obtain product coke with approximately the target particle size, and the product coke has a larger particle size than the conventional method and has the same or higher strength. I can see that you are prepared.
以上説明したように、本発明に係る冶金用コークスの製
造法は上記の構成を有しているものであるから、原料石
炭への微粉コークスの添加量の調整という簡便な手法に
より製品コークスの粒度を冶金炉において要求される品
質或いは操業状況にマツチさせて自由に制御することが
でき、特に、従来困難であった粒度の大きい領域の製品
についても制御加能となり、その工業的価値は極めて大
きいものである。As explained above, since the method for producing metallurgical coke according to the present invention has the above configuration, the particle size of the product coke can be adjusted by a simple method of adjusting the amount of fine coke added to raw coal. can be freely controlled to match the quality or operating conditions required in the metallurgical furnace, and in particular, it is possible to control products with large particle sizes, which was previously difficult, and its industrial value is extremely large. It is something.
第1図は微粉コークス添加量とドラム試験後のコークス
の平均粒径との関係を示す図、第2図は微粉コークス添
加量とコークス強度(D I l530)との関係を示
す図である。
8−FIG. 1 is a diagram showing the relationship between the amount of fine coke added and the average particle diameter of coke after a drum test, and FIG. 2 is a diagram showing the relationship between the amount of fine coke added and coke strength (D I 1530). 8-
Claims (1)
スを添加すると共に、目的とする製品粒度に応じて該微
粉コークスの添加量を調整することによって製品コーク
スの粒度を制御することを特徴とする冶金用コークスの
製造法。A metallurgical product characterized by adding fine coke to raw coal and controlling the particle size of the product coke by adjusting the amount of the fine coke added according to the desired product particle size when producing metallurgical coke. Coke manufacturing method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17773683A JPS6069192A (en) | 1983-09-26 | 1983-09-26 | Preparation of coke for metallurgy |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17773683A JPS6069192A (en) | 1983-09-26 | 1983-09-26 | Preparation of coke for metallurgy |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6069192A true JPS6069192A (en) | 1985-04-19 |
Family
ID=16036221
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17773683A Pending JPS6069192A (en) | 1983-09-26 | 1983-09-26 | Preparation of coke for metallurgy |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6069192A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02127495A (en) * | 1988-11-07 | 1990-05-16 | Nippon Steel Chem Co Ltd | Block coke manufacturing method |
| JP2019031594A (en) * | 2017-08-07 | 2019-02-28 | 関西熱化学株式会社 | Mixing rate determination method and coke manufacturing method |
| JP2025073986A (en) * | 2023-10-27 | 2025-05-13 | Jfeスチール株式会社 | Coke manufacturing method |
| WO2025115362A1 (en) * | 2023-11-29 | 2025-06-05 | Jfeスチール株式会社 | Coke production method |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5441602A (en) * | 1977-09-09 | 1979-04-03 | Fujitsu Ltd | Loop type data delivery system |
| JPS6040192A (en) * | 1983-08-12 | 1985-03-02 | Kansai Coke & Chem Co Ltd | Production of metallurgical coke |
| JPS6047095A (en) * | 1983-08-25 | 1985-03-14 | Nippon Kokan Kk <Nkk> | Method for producing metallurgical coke |
-
1983
- 1983-09-26 JP JP17773683A patent/JPS6069192A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5441602A (en) * | 1977-09-09 | 1979-04-03 | Fujitsu Ltd | Loop type data delivery system |
| JPS6040192A (en) * | 1983-08-12 | 1985-03-02 | Kansai Coke & Chem Co Ltd | Production of metallurgical coke |
| JPS6047095A (en) * | 1983-08-25 | 1985-03-14 | Nippon Kokan Kk <Nkk> | Method for producing metallurgical coke |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02127495A (en) * | 1988-11-07 | 1990-05-16 | Nippon Steel Chem Co Ltd | Block coke manufacturing method |
| JP2019031594A (en) * | 2017-08-07 | 2019-02-28 | 関西熱化学株式会社 | Mixing rate determination method and coke manufacturing method |
| JP2025073986A (en) * | 2023-10-27 | 2025-05-13 | Jfeスチール株式会社 | Coke manufacturing method |
| WO2025115362A1 (en) * | 2023-11-29 | 2025-06-05 | Jfeスチール株式会社 | Coke production method |
| JPWO2025115362A1 (en) * | 2023-11-29 | 2025-06-05 |
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