JPH0621300B2 - Sintering method of iron ore - Google Patents
Sintering method of iron oreInfo
- Publication number
- JPH0621300B2 JPH0621300B2 JP12879985A JP12879985A JPH0621300B2 JP H0621300 B2 JPH0621300 B2 JP H0621300B2 JP 12879985 A JP12879985 A JP 12879985A JP 12879985 A JP12879985 A JP 12879985A JP H0621300 B2 JPH0621300 B2 JP H0621300B2
- Authority
- JP
- Japan
- Prior art keywords
- iron ore
- sintering
- raw materials
- feo
- raw material
- 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
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims description 82
- 229910052742 iron Inorganic materials 0.000 title claims description 41
- 238000005245 sintering Methods 0.000 title claims description 32
- 238000000034 method Methods 0.000 title claims description 12
- 239000002994 raw material Substances 0.000 claims description 27
- 239000004449 solid propellant Substances 0.000 claims description 12
- 235000019738 Limestone Nutrition 0.000 claims description 10
- 239000006028 limestone Substances 0.000 claims description 10
- 238000002156 mixing Methods 0.000 claims description 10
- 239000000428 dust Substances 0.000 claims description 9
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- 239000000292 calcium oxide Substances 0.000 claims description 4
- 235000012255 calcium oxide Nutrition 0.000 claims description 4
- 239000008187 granular material Substances 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 description 8
- 239000000571 coke Substances 0.000 description 7
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 6
- 235000011941 Tilia x europaea Nutrition 0.000 description 6
- 239000004571 lime Substances 0.000 description 6
- 238000007796 conventional method Methods 0.000 description 4
- 230000002829 reductive effect Effects 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 239000007858 starting material Substances 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000005469 granulation Methods 0.000 description 2
- 230000003179 granulation Effects 0.000 description 2
- 229910052595 hematite Inorganic materials 0.000 description 2
- 239000011019 hematite Substances 0.000 description 2
- LIKBJVNGSGBSGK-UHFFFAOYSA-N iron(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Fe+3].[Fe+3] LIKBJVNGSGBSGK-UHFFFAOYSA-N 0.000 description 2
- 238000009766 low-temperature sintering Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000012256 powdered iron Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- WYTGDNHDOZPMIW-RCBQFDQVSA-N alstonine Natural products C1=CC2=C3C=CC=CC3=NC2=C2N1C[C@H]1[C@H](C)OC=C(C(=O)OC)[C@H]1C2 WYTGDNHDOZPMIW-RCBQFDQVSA-N 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- WETINTNJFLGREW-UHFFFAOYSA-N calcium;iron;tetrahydrate Chemical compound O.O.O.O.[Ca].[Fe].[Fe] WETINTNJFLGREW-UHFFFAOYSA-N 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 235000013312 flour Nutrition 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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,鉄鉱石の焼結法に関する。The present invention relates to a method for sintering iron ore.
高炉操業において,焼結鉱の性質特に被還元性(JIS-M87
13に規定の還元率)が良好であることが要求される。一
般に焼結鉱の低温還元粉化性が著しいと高炉シャフト部
の上部(300〜700℃付近)で還元されて粉化し,この粉化
程度が特に著しくなると炉内の通気性が損なわれてスリ
ップ,棚吊りなどを惹起させ炉内を不安定にする。一方
高炉に装入された焼結鉱は塊状で存在する間はCOを主体
とする炉内上昇ガスにより還元され,その後溶解し,未
還元部分は赤熱コークスと直接的に反応して還元され
る。したがって溶解直前の還元率が高いほどコークスの
消費が少なくてすみ,高炉の燃料比を低減させることが
できる。In blast furnace operation, the properties of sinter are especially reducible (JIS-M87
The reduction rate specified in 13) is required to be good. Generally, if the low-temperature reductive pulverization property of sinter is remarkable, it will be reduced and pulverized at the upper part of the blast furnace shaft (around 300 to 700 ° C). , Instability in the furnace is caused by hanging. On the other hand, the sinter charged into the blast furnace is reduced by the ascending gas mainly containing CO while it is present in the form of lumps, and then dissolved, and the unreduced part is directly reacted with the red hot coke to be reduced. . Therefore, the higher the reduction rate immediately before melting, the less the consumption of coke, and the lower the fuel ratio in the blast furnace.
焼結鉱の被還元性を高めるために,焼結鉱の製造にあた
って,コークス粉等を燃料配合率を適切に調節したうえ
焼結温度を旧来の1350〜1450℃から1200〜1300℃程度の
比較的低い温度とし,これによって焼結鉱中のFeOを低
くすることが提案され,実施されている。In order to improve the reducibility of sinter, in the production of sinter, the coke powder was adjusted appropriately for the fuel blending ratio and the sintering temperature was compared from the traditional 1350 to 1450 ℃ to 1200 to 1300 ℃. It has been proposed and is being implemented to lower the FeO content in the sinter by setting a relatively low temperature.
焼結温度を低くしてFeO量を減少させる焼結鉱の製造法
を実施する場合,難溶融性鉄鉱石の使用が制限されると
いう問題が起こる。鉄鉱石は銘柄によって鉱物組成や成
因が異なり,焼結処理に供したときに同化し易いもの,
し難いものがある。例えばオーストラリア産鉄鉱石は一
般に同化し易く,南アフリカ産鉄鉱石は一般に同化し難
い。いろんな事情から,種々の銘柄の鉄鉱石を混合して
焼結に供しているのが実情であるが,焼結過程で同化し
難く天然鉱石のままの形態で焼結鉱中に残存し易い傾向
のある緻密質の難溶融性鉄鉱石を配合した場合には,特
に焼結温度を低くすることによって焼結鉱中のFeOを低
下させようとしても,限界が生じてくる。したがって被
還元性の良好な焼結鉱を得ようとすると,かような難溶
融性鉄鉱石の配合量を制限しなければならなくなる。When carrying out a method for producing a sinter in which the sintering temperature is lowered to reduce the amount of FeO, there arises a problem that the use of refractory iron ore is limited. Iron ores differ in mineral composition and origin depending on the brand, and are easily assimilated when subjected to sintering treatment,
There is something difficult to do. For example, Australian iron ore is generally easy to assimilate, and South African iron ore is generally difficult to assimilate. Under various circumstances, it is the actual situation that various types of iron ore are mixed and used for sintering, but it is difficult to assimilate during the sintering process and tend to remain in the sintered ore in the form of natural ore. In the case of blending a dense and refractory iron ore with a certain amount, even if it is attempted to lower the FeO content in the sintered ore by lowering the sintering temperature, there will be a limit. Therefore, in order to obtain a sinter having good reducibility, it is necessary to limit the compounding amount of such refractory iron ore.
本発明は,かような難溶融性鉄鉱石を配合しても良好な
被還元性をもつ焼結鉱を従来と同様の焼結条件で製造す
ることを目的とするものである。An object of the present invention is to produce a sinter having a good reducibility even if such a refractory iron ore is blended under the same sintering conditions as the conventional one.
本発明は、複数の銘柄からなる鉄鉱石を主原料とし,こ
れに,雑原料(例えば返鉱),副原料および固体燃料を
混合して焼結原料を得るにさいし,前記の目的を達成す
る処方として、前記したような難溶融性鉄鉱石の銘柄を
他の鉄鉱石の銘柄から選り分け,この選り分けた難溶融
性鉄鉱石に,副原料の一部としての石灰石または石灰石
と生石灰,固体燃料の一部としてのコークス粉,および
製鉄所で発生する含FeOダストを混合して混合物中のFeO
含有率を0.2重量%以上としたうえ,これに水を添加し
て造粒し,この造粒物を,残りの銘柄の鉄鉱石,返鉱,
副原料および固体燃料に配合して焼結原料とし,得られ
た焼結原料を焼結機に供給して焼結することを特徴とす
る。The present invention achieves the above-mentioned object when an iron ore composed of a plurality of brands is used as a main raw material, and a miscellaneous raw material (for example, return ore), an auxiliary raw material and a solid fuel are mixed to obtain a sintering raw material. As a prescription, the above-mentioned refractory iron ore brands are selected from other iron ore brands, and the selected refractory iron ores are mixed with limestone or limestone and quick lime as a part of auxiliary materials, and solid fuel. FeO in the mixture by mixing coke powder as a part and FeO-containing dust generated in the steel mill
The content was adjusted to 0.2% by weight or more, and water was added to this to granulate, and the granulated product was used as the remaining brand of iron ore, return ore,
It is characterized in that it is mixed with the auxiliary raw material and the solid fuel to obtain a sintering raw material, and the obtained sintering raw material is supplied to a sintering machine for sintering.
ここで「難溶融性鉄鉱石」とは,前述したように,従来
法により1200〜1300℃の焼結温度で焼結したさいに焼結
過程で同化しがたく天然鉱石のままの形態で焼結鉱中に
残存する傾向のある緻密質の難溶融性の鉄鉱石を言う。
また本発明法は従来より広く使用されているドワイトロ
イド式焼結機を用いて焼結することを前提としている。Here, "hardly soluble iron ore" means, as described above, a natural ore that is hard to assimilate during the sintering process when sintered by the conventional method at a sintering temperature of 1200 to 1300 ° C. It is a dense, infusible iron ore that tends to remain in the ore.
Further, the method of the present invention is premised on sintering using a Dwightroid type sintering machine which has been widely used.
より具体的に説明すると,主原料鉄鉱石の各銘柄のう
ち,緻密質の難溶融性鉄鉱石については,これを粉状の
まま配合するのではなく,石灰,コークスおよび含FeO
ダストと共に造粒してから配合するのである。この造粒
のさいに難溶融性鉄鉱石と共に配合する石灰は,石灰石
単独であってもよいが石灰石と生石灰とを複合して使用
してもよく,これは,もともと全焼結原料中に配合予定
の副原料の一部としてこの造粒品中に存在させることが
できる。また造粒品中に存在させるコークス粉について
も,全焼結原料中に配合予定の固体燃料の一部として存
在させる。More specifically, among the main raw iron ore brands, the dense refractory iron ore is not blended as it is in powder form, but lime, coke and FeO
It is blended after granulating with dust. The lime compounded with the refractory iron ore at the time of this granulation may be limestone alone, or may be a mixture of limestone and quick lime, which is originally planned to be compounded in all sintering raw materials. It can be present in this granulated product as part of the auxiliary raw material. In addition, the coke powder that is present in the granulated product is also present as a part of the solid fuel to be blended in all the sintering raw materials.
この造粒品中に含FeOダストを添加することが本発明の
一つの特徴である。製鉄所内で回収しているダスト類
は,その一例を第1表に示したように,かなりの量のFe
Oを含有しているのが通常である。本発明ではこのよう
な含FeOダストを難溶融性鉄鉱石に石灰,コークスと共
に配合し,FeO量が0.2 %以上となるような造粒物とす
る。One of the features of the present invention is to add FeO-containing dust to the granulated product. As shown in Table 1, an example of the dust collected in the steel mill is
It usually contains O. In the present invention, such FeO-containing dust is mixed with refractory iron ore together with lime and coke to form a granulated product having a FeO content of 0.2% or more.
この含FeOダストを,石灰,コークスと共に緻密質な難
溶融性鉄鉱石と混合して造粒することにより,この難溶
融性鉄鉱石粒子の直近にFeO,石灰およびコークスが存在
することになるので,これを焼結原料中に配合して焼結
処理したさいに,低融点の融液を造粒物中の難溶融性鉄
鉱石粒子の周囲に形成させることができ,この溶融中へ
難溶融性鉄鉱石の同化を促進させることができる。これ
によって,従来の低温焼結法では巨大なヘマタイト結晶
として天然鉱石のまま焼結品中に残存するようなもの
も,同じ低温焼結条件下であってもカルシウムフエライ
トおよび微細なヘマタイトに変化させることができるこ
とになり,被還元性の良好な焼結鉱を得ることができる
ことが判明した。 By mixing this FeO-containing dust with dense refractory iron ore together with lime and coke and granulating, FeO, lime and coke will exist in the immediate vicinity of the refractory iron ore particles. , When this is blended in the sintering raw material and sintered, a low-melting point melt can be formed around the refractory iron ore particles in the granulated material. It can promote the assimilation of natural iron ore. As a result, even if the natural ore that remains in the sintered product as a huge hematite crystal in the conventional low temperature sintering method is changed into calcium ferrite and fine hematite even under the same low temperature sintering conditions. Therefore, it was found that a sintered ore with good reducibility can be obtained.
第1図は,本発明に従う製造工程のフロー図である。右
側のAで示す基本フローにおける4種の出発材料である
粉状鉄鉱石,返鉱,副原料および固体燃料のうち,緻密
質難溶融性鉄鉱石を選り分けてBの系統に使用する。こ
のB系統において使用する石灰石(または石灰石と生石
灰)と固体燃料はA系統の副原料の一部および固体燃料
の一部をこのB系統にまわすことができる。B系統にお
いては,先ず難溶融性鉄鉱石,石灰およびコークス粉に
含FeOダストを混合物中のFeO含有量が0.2重量%以上と
なるように混合し、水を添加して造粒する。そして,得
られた造粒品を,Aの4種の出発材料である粉状鉄鉱
石,返鉱,副原料および固体燃料を共に混合するか,ま
たはこの4種の出発材料を混合したものに混合する。こ
こで副原料とは蛇紋岩,珪砂,石灰石などを指す。固体
燃料は通常はコークス粉である。FIG. 1 is a flow chart of a manufacturing process according to the present invention. Of the four starting materials in the basic flow indicated by A on the right side, which are the powdery iron ore, the return ore, the auxiliary raw material, and the solid fuel, the dense refractory iron ore is selected and used for the system B. The limestone (or limestone and quick lime) and the solid fuel used in the B system can pass a part of the auxiliary raw material of the A system and a part of the solid fuel to the B system. In the system B, first, the refractory iron ore, lime, and coke powder are mixed with FeO-containing dust so that the FeO content in the mixture is 0.2% by weight or more, and water is added for granulation. Then, the obtained granulated product is mixed with powdered iron ore which is four kinds of starting materials of A, return ore, auxiliary raw materials and solid fuel together, or a mixture of these four kinds of starting materials. Mix. Here, the auxiliary material refers to serpentine, silica sand, limestone, and the like. The solid fuel is usually coke flour.
実施例1 第2表に本例の焼結原料の配合割合を示した。第2表中
の従来法(A0)は,第1図におけるA系統だけに相当
するものであり,この場合には,粉状鉄鉱石原料に緻密
質の難溶融性鉄鉱石もそのまま配合したものである。第
2表中のBは,第1図のように,粉状鉄鉱石のうちから
難溶融性鉄鉱石を選り分け,これにA系統中の石灰石お
よびコークス粉の一部をとり,更に含FeOダストを配合
したものである。このBは水を加えて造粒したあと,第
1図のフローに示すように,第一ミキサーで他の原料と
共に混合した。従来法および本発明法とを焼結原料を同
じ焼結機に装填し,両者とも同じ焼結条件のもとで焼結
した。得られた焼結鉱をJIS-M8713に準拠した試験に供
しその還元率を調べた。その結果を第3表に示した。ま
た生産率も第3表に示した。Example 1 Table 2 shows the mixing ratio of the sintering raw material of this example. The conventional method (A 0 ) in Table 2 corresponds only to the A system in FIG. 1, and in this case, the powdery iron ore raw material was also blended with the dense refractory iron ore as it was. It is a thing. As shown in Fig. 1, B in Table 2 selects the refractory iron ore from the powdered iron ore, and takes a part of the limestone and coke powder in the system A, and further contains FeO dust. It is a mixture of. This B was granulated by adding water and then mixed with other raw materials in the first mixer as shown in the flow chart of FIG. The sintering raw materials of the conventional method and the method of the present invention were loaded in the same sintering machine, and both were sintered under the same sintering conditions. The obtained sinter was subjected to a test according to JIS-M8713, and its reduction rate was investigated. The results are shown in Table 3. The production rate is also shown in Table 3.
第3表の結果より,本発明法によると従来法に比べて同
じ生産率のもとで還元率は約3%上昇した焼結鉱が得ら
れたことがわかる。From the results of Table 3, it can be seen that according to the method of the present invention, a sinter having a reduction rate increased by about 3% was obtained under the same production rate as in the conventional method.
実施例2 易溶融性のオーストラリア産の鉄鉱石の配合割合を減少
し,難溶融性の南アフリカ産の鉄鉱石の配合割合を増加
させたこと,そして含FeOダストとしてFeO含有量が異な
るものを使用したこと以外は,実施例1と同じようにし
て5種類の焼結原料を作り,これらを同じ焼結条件のも
とで焼結した。その配合割合を実施例1と同様の基準で
第4表に示した。また,各々の焼結品の生産率と還元性
を第5表に示した。 Example 2 The blending ratio of easily meltable Australian iron ore was decreased and the blending ratio of refractory South African iron ore was increased, and FeO-containing dusts having different FeO contents were used. Except for the above, five kinds of sintering raw materials were prepared in the same manner as in Example 1, and these were sintered under the same sintering conditions. The blending ratio is shown in Table 4 on the same basis as in Example 1. Table 5 shows the production rate and reducibility of each sintered product.
第5表の結果から,本発明法によると,難溶融性鉄鉱石
の配合割合を約18%と多くした場合でも生産率を低下さ
せることなく還元率を上昇できたことがわかる。From the results in Table 5, it can be seen that according to the method of the present invention, the reduction rate could be increased without lowering the production rate even when the blending ratio of the refractory iron ore was increased to about 18%.
【図面の簡単な説明】 第1図は本発明法の製造工程を説明するための工程図で
ある。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a process drawing for explaining the manufacturing process of the method of the present invention.
Claims (1)
これに,雑原料,副原料および固体燃料を混合して焼結
原料を得るにさいし, 難溶融性鉄鉱石の銘柄を他の鉄鉱石の銘柄から選り分
け, この選り分けた難溶融性鉄鉱石に,前記の副原料の一部
としての石灰石または石灰石と生石灰,固体燃料の一部
としてのコークス粉,および製鉄所で発生する含FeOダ
ストを混合して混合物中のFeO含有率を0.2重量%以上と
し,そしてこれに水を添加して造粒し, この造粒物を,残りの銘柄の鉄鉱石,雑原料,副原料お
よび固体燃料に配合して焼結原料とし, 得られた焼結原料を焼結機に供給して焼結することから
なる鉄鉱石の焼結法。1. A main raw material is iron ore composed of a plurality of brands,
In mixing this with miscellaneous raw materials, auxiliary raw materials and solid fuel to obtain a sintering raw material, the brands of refractory iron ore are selected from the brands of other iron ores, and the selected refractory iron ores are Limestone or limestone as a part of the above-mentioned raw materials and quicklime, coke powder as a part of solid fuel, and FeO-containing dust generated in the iron mill are mixed to make the FeO content in the mixture 0.2% by weight or more. Then, water was added to this to granulate, and the granulated material was blended with the remaining brands of iron ore, miscellaneous raw materials, auxiliary raw materials, and solid fuel to obtain a sintering raw material. Sintering method of iron ore consisting of supplying to a sintering machine and sintering.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12879985A JPH0621300B2 (en) | 1985-06-13 | 1985-06-13 | Sintering method of iron ore |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP12879985A JPH0621300B2 (en) | 1985-06-13 | 1985-06-13 | Sintering method of iron ore |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61288022A JPS61288022A (en) | 1986-12-18 |
| JPH0621300B2 true JPH0621300B2 (en) | 1994-03-23 |
Family
ID=14993719
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12879985A Expired - Lifetime JPH0621300B2 (en) | 1985-06-13 | 1985-06-13 | Sintering method of iron ore |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0621300B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109652643B (en) * | 2019-01-30 | 2020-09-01 | 中南大学 | High-quality sinter for COREX smelting reduction ironmaking process and preparation method thereof |
-
1985
- 1985-06-13 JP JP12879985A patent/JPH0621300B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61288022A (en) | 1986-12-18 |
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