TWI299363B - Method for manufacturing sintered dre - Google Patents

Method for manufacturing sintered dre Download PDF

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TWI299363B
TWI299363B TW94134179A TW94134179A TWI299363B TW I299363 B TWI299363 B TW I299363B TW 94134179 A TW94134179 A TW 94134179A TW 94134179 A TW94134179 A TW 94134179A TW I299363 B TWI299363 B TW I299363B
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ore
iron ore
amount
iron
sintered
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TW94134179A
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TW200617182A (en
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Oyama Nobuyuki
Sato Hideaki
Machida Satoshi
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Jfe Steel Corp
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    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • C22B1/14Agglomerating; Briquetting; Binding; Granulating
    • C22B1/16Sintering; Agglomerating
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • C22B1/14Agglomerating; Briquetting; Binding; Granulating
    • C22B1/16Sintering; Agglomerating
    • C22B1/20Sintering; Agglomerating in sintering machines with movable grates

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Organic Chemistry (AREA)
  • Metallurgy (AREA)
  • Materials Engineering (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Description

1299363 九、發明說明: 【發明所屬之技術領域】 ·、本%明係關於用以作為高爐等之主原料的燒結礦之製 造方法。 【先前技術】 冋爐的主原料之燒結礦,通常可如下述般製造。首先, 於粉鐵礦石中配合以石灰粉等之含Ca0之副原料、石夕石或 蛇,岩等之含S1Q2之副原料及焦炭粉等之碳材,對其加入 適里的水進行此合並造粒。將此造粒成之配合原料(燒結 原❹真充到德外特洛伊德式燒結機之墊板(pallet)上至 无疋的厚度冑此填充床表層部的碳材點火後,一邊由下 方吸引空氣’-邊使填充床内部的碳材燃燒,藉由此辦燒 熱對配合原料進行燒結得到燒結餅(cake)。然後,再對此 燒結餅進行粉碎並整粒,得到粒徑為數丽以上之成品燒 結礦。 為女疋地進行尚爐作業,須有高品質的燒結礦。通常, 品質· shu 11 er強度(冷間強度)、還原粉化指 ㈣DI) '被㈣性(RI)等作為指標,以此等為指標之成 品燒結礦的品質,對高爐操作之原料饋料狀態之安定性、 爐内通氣性與通液性、礦石之還原效率、高溫性狀等有大 的影響。因此,於燒結礦的製程中須進行嚴格的品質管 f。又,為減低燒結礦之製造成本,須謀求燒結 ^提高,並_求燒結礦®造狀效率化與生產性之提 312XP/發明說明書(補件)/94_丨2/94 m】79 5 1299363 然而,燒結礦之原料鐵礦石,以往主要係使用赤鐵礦 (hematite)與磁鐵礦(magnetite),最近,由於此等良質 的鐵礦石之供給量逐漸減少,以致於使用褐鐵礦礦石與馬 拉曼巴(Marra Mamba)礦石(皆為澳洲產鐵礦石)等之結晶 ^ 水含有量高的鐵礦石之必要性日益迫切,將來其使用量勢 必曰益增大。此處,所謂馬拉曼巴礦石係產自澳洲的馬拉 曼巴礦床的鐵礦石之總稱。通常為以針鐵礦(Goethite) • (Fe2〇3· H2O)與赤鐵礦(martite)(具有磁鐵礦構造之Fe2〇3) 為主要礦物,且以5%左右之高含有率含有結晶水的礦石。 以品名稱之則有西安吉拉斯(West Angel as)礦、MAC礦等 代表性的鐵礦石。又,褐鐵礦礦石的代表例為豆石 (pisolite)礦石。此豆石礦石,通常為含有在魚卵狀的赤 鐵礦(Fe2〇3)的間隙埋入著針鐵礦(Fe2〇3 · H2〇)之内部構 造、且以8%左右之高含有率含有結晶水的礦石。以品名 稱之則有羅布立巴(Robe River)礙、揚迪克吉那 (Yandicoogina)礦等代表性的鐵鑛石。 ^ 又,相對於上述各種鐵礦石般之P含有量未滿0. 10質 量%(通常為0.06質量%以下)的鐵礦石,通常,將P含有 量0 · 10質量%以上之鐵礦石稱為高構礦石。以此種P含有 量高的鐵礦石作為高爐原料使用時,所製造的鐵水之P濃 " 度較高,會使脫磷處理的負荷增大,故以往幾乎不被使 - 用。然而,由於如上述般良質的鐵礦石之供給量日益減 少,於燒結原料中配合相當量的此種高磷礦石亦受到檢討 中〇 6 312XP/發明說明書(補件)/94-12/94134179 1299363 ; 门、、、口日日水礦石作為燒結原料之情況下,被指出 問題’其為:⑴由於對於燒結時結晶水脫離時之 應須有熱補償,故相應於此部》,配合之碳原料 ^ 厌等)必柄量;⑵因結晶水之脫離,於溶融反 中生成的炫融液會引起局部的過炫融反應,其結果 g v致生產性與成品產率降低。 又’曾被指出之問題為:尤其於馬拉曼巴礦石中,由 於微粉份大多造粒性差劣,致使燒結床(燒結原料層)内的 性變差而降低成品強度,並伴隨著引發生產率盥 產率降低等之問題。 丨〜玍座手一成.口1299363 IX. Description of the invention: [Technical field to which the invention pertains] The present invention relates to a method for producing a sintered ore which is used as a main raw material of a blast furnace or the like. [Prior Art] The sintered ore of the main raw material of the crucible furnace can be usually produced as follows. First, the powdered iron ore is blended with a raw material containing Ca0 such as lime powder, a raw material containing S1Q2, and a carbon material such as coke powder, such as a stone or a snake, a rock, and the like, and added with appropriate water. This combined granulation. The granulated material is sintered into a raw material (sintered raw sputum is poured onto a pallet of a German-outer Troyd type sintering machine to a thickness of no 疋, and the carbon material in the surface layer of the packed bed is ignited, and then attracted from below. The air is burned to the inside of the packed bed, and the sintered raw material is sintered to obtain a cake. Then, the sintered cake is pulverized and sized to obtain a particle size of several or more. Finished sinter. For high-quality sinter ore, it is necessary to have high-quality sinter. In general, quality, shu 11 er strength (cold strength), reduction pulverization (4) DI) 'is (IV) (RI), etc. As an indicator, the quality of the finished sinter with this index as a target has a great influence on the stability of the raw material feeding state of the blast furnace operation, the ventilation property and the liquid permeability in the furnace, the reduction efficiency of the ore, and the high temperature property. Therefore, strict quality control f must be carried out in the process of sinter. In addition, in order to reduce the manufacturing cost of the sinter, it is necessary to improve the sintering, and to improve the efficiency and productivity of the sinter ore 312XP/invention specification (supplement)/94_丨2/94 m] 79 5 1299363 However, the raw material iron ore of sinter has mainly used hematite and magnetite. Recently, the supply of such good iron ore has gradually decreased, so that lignite is used. The crystallization of mineral ore and Mara Mamba ore (all of which is iron ore produced in Australia) is increasingly urgent for iron ore with high water content, and its use will inevitably increase in the future. Here, the so-called Maramanba ore is a general term for iron ore produced in the Maramamba deposit in Australia. It is usually made of goethite (Fe2〇3·H2O) and martite (Fe2〇3 with magnetite structure) as the main mineral, and contains crystals at a high content of about 5%. The ore of water. The name of the product is representative of iron ore such as the West Angel as mine and the MAC mine. Further, a representative example of the limonite ore is a pistolite ore. This bean ore is usually embedded in the internal structure of goethite (Fe2〇3 · H2〇) in the gap of hematite (Fe2〇3), and has a high content of about 8%. An ore containing crystal water. In the name of the product, there are representative iron ore such as the Robe River barrier and the Yandigogina mine. Further, iron ore having a P content of less than 0.10% by mass (usually 0.06 mass% or less) as compared with the above various iron ores, usually, an iron ore having a P content of 0. 10% by mass or more Stone is called high ore. When such iron ore having a high P content is used as a blast furnace raw material, the P richness of the produced molten iron is high, and the load of the dephosphorization treatment is increased, so that it has hardly been used in the past. However, due to the decreasing supply of good quality iron ore as described above, the amount of such high-phosphorus ore blended in the sintered raw material has also been reviewed. 〇6 312XP/Invention Manual (supplement)/94-12/94134179 1299363 ; In the case of the water, ore, as the sintering raw material, the door, and the mouth are pointed out as 'the problem': (1) Since the crystallization water should be detached during the sintering, it should be thermally compensated, so corresponding to this section, Carbon raw materials ^ 厌, etc.) must be handled; (2) due to the crystallization of water, the molten liquid formed in the melt reaction will cause local over-sweet reaction, and the result is that gv-induced productivity and finished product yield are reduced. 'The problem that has been pointed out is that, especially in the minerals of Malamamba, the fineness of the fine powder is mostly poor, which causes the deterioration in the sintered bed (sintering raw material layer) to lower the strength of the finished product, accompanied by the productivity. Problems such as reduced yields.丨~玍座手一成.口

士又白知於使用微粉份多的馬拉曼巴礦石製造燒結礦 日寸’為強化藉由混合㈣之造粒,曾有提案提出對配合^ 馬拉曼巴礦石的燒結原料進行高速㈣以進行混合、造球 的技術(專利文獻丨:日本專利特開平7_331342號公報) 然而,由於專利文獻1之技術必須特別的攪拌手抨, =有設備成本與處理成本增加之問題。又,依據本發則 等之檢討’發現:即使如專利文獻丨般使配合有馬拉 礦石的燒結原料之造粒強化,未必能提高生產性與成^ 率’又’尤其於多量配合馬拉曼巴礦石之情況下 到冷間強度(shutter強度)非常低的燒結礦。” b ' 又’關於高鱗礦石,由於以往幾乎沒有作為燒 之使用實績’故於燒結原料中配合相當量的情形下=、姓 礦的品質與生產性、成品產率的影響之相關檢討 = 如。因此’本發明者料對高翻狀配合料燒結礦的 312ΧΡ/發明說明書(補件)/9木12/94134179 7 1299363 品質等之影響進行查察與檢討,結果發現高磷礦石的配合 量若增加,燒結礦的冷間強度與生產性有降低之傾向。 【發明内容】 本發明之目的在於提供燒結礦之製造方法,其係與配 合於燒結原料中的原料礦石種類無關而可製造高品質燒 結礦者,亦即,即使於配合相當量的高磷礦石或馬拉曼巴 礦石之時,亦能以高生產性與高成品產率製造冷間強度高 的南品質燒結礦。Shi Baibai knows that the use of micro-powdered Maramamba ore to make sinter ore is to strengthen the granulation by mixing (4). It has been proposed to carry out the high-speed (four) of the sintering raw materials of the Maramamba ore. In the technique of the patent document 1, the technique of the patent document 1 requires a special stirring of the handcuffs, and there is a problem that the equipment cost and the processing cost increase. In addition, according to the review of this issue, etc., it was found that even if the granulation strengthening of the sintering raw material with the malad ore is carried out as in the patent document, the productivity and the yield are not necessarily improved. In the case of Ba ore, the sinter is very low in cold strength (shutter strength). "b' and 'about" high-grade ore, because there is almost no use as a result of burning in the past, so in the case of a considerable amount of sintering raw materials =, the quality of the surname mine and the impact of productivity, finished product yield = Therefore, the inventors of the present invention investigated and reviewed the effects of 312ΧΡ/inventive specification (supplement)/9 wood 12/94134179 7 1299363 quality of high-floating batch sinter, and found that the cooperation of high-phosphorus ore was found. When the amount is increased, the cold strength and productivity of the sintered ore tend to be lowered. SUMMARY OF THE INVENTION An object of the present invention is to provide a method for producing a sintered ore which can be produced irrespective of the type of raw ore to be blended in a sintered raw material. High-quality sinter mines, that is, even in the case of blending a considerable amount of high-phosphorus ore or malamamba ore, can produce high-quality cold-sintered south-quality sinter with high productivity and high finished product yield.

如上述般於燒結原料中配合多量的馬拉曼巴礦石時, 以專利文獻1所示之強化燒結原料的造粒之方法,成品燒 結礦的冷間強度、生產性與成品產率之改善未必有充分的 效果,此情形意味著本質上的問題並非在原料的造粒性, 而是在於其他的因素。因此,本發明者等為探究此部分而 做了各種實驗,同時亦針對高磷礦石的配合對於成品燒結 礦的品質等之影響及其改善對策也做了各種檢討,結果發 現下述之事實: (1)作為燒結原料之鐵礦石,不論其種類為何,原本礦 石粒子内部具有微細氣孔,而馬拉曼巴礦石之微細氣孔量 較其他礦石格外多。因此,燒結過程中所生成的熔融液會 浸透到原本即有的微細氣孔中,使得用以結合礦石粒子間 之熔融液不足,其結果使得成品燒結礦之冷間強度大幅降 低0 (2)由於上述般的礦石粒子内部的微細氣孔與熔融液 的關係,成品燒結礦的冷間強度係依存於配合在燒結原料 8 312XP/發明說明書(補件)/94-12/94134179 1299363 中的原料礦石之平均氣孔量,因而,不論 燒'=中之綱石的平均氣孔量成 下可有效地提咼成品燒結礦的冷間強 度0 2因而,即使於多量配合馬拉曼巴礦石之情況下,夢 广當地選擇、調整所配合的其他礦石之種類或其配人9 率’使配合於燒結補中的原料礦石之平均氣孔量在既口 白勺水準以下,則可依高生產性與高成品產率 度的高品質燒結礦。 〇 7間強 (4)另一方面,於燒結原料中配合高磷礦石時,配人 碟礦石對成品燒結礦的品f等之影響並無法單從該礦^ 的氣孔量來評估。亦即’高鄉石的平均氣孔量雖大 ,鐵=與馬拉曼巴礦石之中間程度,但即使依據此種㈣ 乳孔量將高鱗礦;5㈣上述⑶的基準配合 充分的冷間強度。 …、去件到 • (5)其理由在於’高磷礦石除了微粉的比例較多之外, 與其他礦石相較其微粉中Ah〇3含有量相當高,由於此等 j因使得燒結床内通氣性變差,而導致燒結礦的冷間強戶 變差。因而,於配合高磷礦石時,除了該氣孔量:影塑: 外上述諸點之影響亦須加以斟酌。 、 〜本發明係基於上述發現而作成者,其特徵如下· -[1]-種燒結礦之製造方法’係由配合了作為原料礦石 的至少一部份之選自:鐵礦石A,係以水銀壓入測定法 疋之平均氣孔量為0. 03〜〇. 〇5cm3/g(其中,丸粒礦料’ 312XP/發明說明書(補件)/94-12/94134179 9 1299363 (pellet feed)除外);鐵 〇」〇〜。.崎;鐵礦石 0.07〜o.ow/g;中之至少、之平均氣孔量為 B、C為排除p含有量為 的旦鐵礦石(其中,鐵礦石A、 2.0質量%以上者)、與;含有:里:以上且Al2。1含有量為 含有量為2.〇 f量%以 =G.1Q質量%以上且Al2〇3 礦者;其特徵在於,、载廣石D之燒結原料製造燒結When a large amount of Maramanba ore is blended in the sintering raw material as described above, the improvement of the cold strength, productivity, and finished product yield of the finished sintered ore may not be improved by the method of granulating the sinter raw material shown in Patent Document 1. There is a sufficient effect, and this situation means that the essential problem is not in the granulation of the raw material, but in other factors. Therefore, the present inventors conducted various experiments for exploring this part, and also conducted various reviews on the influence of the cooperation of high-phosphorus ore on the quality of the finished sintered ore and the improvement measures, and found the following facts: (1) Iron ore as a raw material for sintering, regardless of its type, the original ore particles have fine pores inside, and the fine pores of the Maramanba ore are much more than other ores. Therefore, the molten liquid formed during the sintering process is soaked into the original fine pores, so that the melt between the ore particles is insufficient, and as a result, the cold strength of the finished sintered ore is greatly reduced. The relationship between the fine pores inside the ore particles and the melt, and the cold strength of the finished sintered ore depends on the raw ore blended in the sintered raw material 8 312XP / invention specification (supplement) / 94-12/94134179 1299363 The average amount of pores, therefore, regardless of the average pore volume of the stone of the burning '= Zhongshi can effectively improve the cold strength of the finished sinter 0 2, thus even in the case of a large amount of Maramanba ore, dream Widely select and adjust the type of other ores to be matched or the ratio of the ratio of the others. The average pore volume of the raw ore blended in the sintering supplement is below the level of the mouth, which can be based on high productivity and high yield. High quality sinter of the rate. 〇 7 strong (4) On the other hand, when the high-phosphorus ore is blended in the sintering raw material, the influence of the matching disc ore on the finished product of the sintered ore can not be evaluated from the porosity of the ore. That is, the average stomatal amount of 'Gaoxiangshi is large, iron=between the Maramamba ore, but even according to the (4) milk hole volume, the high-scale ore; 5(4) the above (3) benchmark with sufficient cold strength . (5) The reason is that 'the high phosphate ore has a higher proportion of the fine powder than the other ores, and the content of Ah〇3 in the fine powder is quite high, because of this j The aeration is deteriorated, and the cold room of the sinter is deteriorated. Therefore, in addition to the amount of pores: the shape of the pores: the influence of the above points must also be considered. The present invention is based on the above findings and is characterized as follows: - [1] - a method for producing a sintered ore" is selected from the group consisting of iron ore A, which is at least a part of a raw material ore. The average pore volume of the mercury intrusion measurement method is 0. 03~〇. 〇5cm3/g (wherein, the pellet mineral material '312XP/invention specification (supplement)/94-12/94134179 9 1299363 (pellet feed) Except); ..; iron ore 0.07~o.ow/g; at least, the average amount of pores is B, C is the iron ore excluding the p content (where iron ore A, 2.0% by mass or more) ), and; contains: Li: above and Al2. 1 content is 2. The amount of 〇f is more than = G.1Q% by mass and Al2〇3 ore; characterized by, sintering of the feldspar D Raw material manufacturing sintering

以由下述式(1): x [Βο/〇] + 0· 〇8 · ···式⑴ χ 平均氣孔量χ=0· 04 x [A%] + 0· u [C%] + 2. Ο x 0. 〇6 χ [〇%] (其中, [A%]:[鐵礦石Α量]/[鐵鑛石Α、β、c、k [B%]:[鐵礦石B量]/[鐵確石A、β、c、d之: [c%]:[鐵礦石c量]/[鐵礦石a、b、c、d之二十量 [鐵礦石D量]/[鐵礦石A、B、c、D^f十量]) •所定義之鐵礦石的平均氣孔量χ成為〇 〇9cm3/g以下之方 式,以配合了鐵礦石之燒結原料製造燒結礦。 [2] 於上述Π]之製造方法中,燒結原料中係配 石B。 八 [3] 於上述[1]之製造方法中,燒結原料中係配合鐵礦 ‘石A、鐵礦石b及鐵礦石C。 八 〃 [4]於上述[2]或[3]之製造方法中,鐵礦石6對於鐵礦 石A、鐵礦石β、鐵礦石c及鐵礦石])之合計量的比例為 20質量%以上。鐵礦石Β的比例以20〜70質量%為佳,尤 1 】2ΧΡ/發明說明書(補件)/94-12/94134179 1299363 以20〜60質量%為更佳。 [5]於上述[2]〜[4]之任一製造方法中,鐵礦石D對於 鐵礦石A、鐵礦石B、鐵礦石C及鐵礦石D之合計量的比 例為20質量%以上。鐵礦石D的比例以20〜60質量%為佳, “ 尤以20〜50質量%為更佳。 此處,本發明所規定的鐵礦石之平均氣孔量,為針對 粒徑4〜7mm的礦石,藉由使用水銀壓入式細孔分布測定裝 置之水銀壓入測定法(壓入壓力:0. 007〜412MPa)測得之微 鲁細氣孔量之平均值(N=10的平均值)。又,上述壓入壓力 範圍為可測定細孔徑0.035〜200 //m之氣孔量的壓力,藉 由在此壓力範圍内進行測定,使用通常的水銀壓入式細孔 分布測定裝置,可正確地測定本發明對象之鐵礦石A〜C及 鐵礦石D的微細氣孔量。 依據本發明,藉由調整屬於燒結原料中所配合之原料 礦石的平均氣孔量且考慮高磷礦石的特殊性所定義之特 定平均氣孔量,不論原料礦石的種類皆可製造高品質之燒 ®結礦;亦即,即使於配合相當量的高磷礦石及/或馬拉曼 巴礦石時,亦能以高生產性與高成品產率製造高冷間強度 之高品質燒結礦。 【實施方式】 。茲針對高磷礦石以外的鐵礦石(鐵礦石A〜C)之配合條 ^ 件加以說明。 圖1表示於使用實機之燒結礦的製造試驗中,改變原 料礦石中的馬拉曼巴礦石之配合比例,調查燒結礦的生產 312XP/發明說明書(補件)/94· 12/94134179 1299363 :中^馬;krf率之、、"果。此作業(全程3日)中,使原料礦石 2所」、、又巴礦石與普通礦石之赤鐵礦石之配合比,如圖 '質旦y :作下述3種水準之變化:(a)赤鐵礦礦石:1〇〇 20貝赤鐵礦礦石:⑽請、馬拉曼巴礦石: 造粒^法及造粒條件將燒結原料 屬礦係使用貿因心ΐ 係使用MAc礦,又,赤鐵 條件俜一^〜(M°untNewman)礦。其他製造與作業 機料::生石灰比例:2·。·、燒結 度.580·,又,調整燒結原料中的石灰 風細I: 查、白雲石之配合比例以使燒結礦之化 =量%。、二 Sl〇2. 5/1 質量%、CaO: 10.2 質 f:%、MgO: 1.〇 :圖、1’隨著原料礦石中之馬拉曼巴礦石的配合比例 二加’成品燒結石廣之生產率與產率降低。就其理由進行 厂丁、之結果’可確認得知:若馬拉曼巴礦石之配合比例增 ° ’則燒結叙冷間強度降低’其結果會導致生產率之降 °表示使用只機之燒結礦之製造中,使原料礦石中 之H以下述2種水準進行操化:⑷微粉之赤鐵礦:約 貝里%其他礙石·(以赤鐵礦礦石為主體之普通礦石): 約9〇質m)馬拉曼巴礦石:約1G f量%、其他礦石(以 赤鐵礦礦石為主體之普通礦石):約90質量%,就成品燒 312XP/發明說明書(補件)/94-12/94134179 12 1299363 « 爆 # 強度)與生產率等之變化進行查 粒^ n中’係將衆原料姨石中的微粉镇(丸 換成原 =。::二1τ %的燒結原料,=1« 之❹比例為約10質量 造粒性的造粒法(所謂卿法)紅^^用強化原料之 造燒結礦。 HPS法)進仃燒結原料之造粒以製 依據圖3之結果,相對於原料礦 丸粒礦料)的(她-,於;其::: 冷間強度一強度)大幅降低,幾二 由以^圖丨及圖3的結果可確認得知:與造粒方法 或^立條件無關,於以-定程度的配合比例配合了馬拉曼 巴,石時,成品燒結礦的冷間強度會降低。此處,已知馬 f ^ =礦石與其他鐵衫比較,其礦石粒子㈣之微細氣 孔非吊多’認為此等存在於礦石粒子内部之微細氣孔,會 影響燒結過程中所生成的溶融液之行為,而對成品燒結礦 的冷間強度造成不良影響。因此,使用具備試驗_1〇〇_ χ__)與X射線α裝置之圖4所示之試驗裝置,對配合 了表1所示之原料礦石的燒結原料進行燒成(燒結中風 速.0. 29Nm/s、焦炭比:5, 5%、混合原料中㈤比:9. ^、 混合原料中Si〇4 : 5.0%、原料粒度:_3腿),將燒結過 程中之原料礦石及燒結餅的氣孔構造與炫融液流 動狀況 312XP/發明說明書(補件)/94_ 12/94134179 1299363 進行解析。 [表1 ]The following formula (1): x [Βο/〇] + 0· 〇8 · ··· (1) χ average pore volume χ=0· 04 x [A%] + 0· u [C%] + 2 Ο x 0. 〇6 χ [〇%] (where, [A%]: [iron ore volume] / [iron ore Α, β, c, k [B%]: [iron ore B amount ] / [Italian stone A, β, c, d: [c%]: [iron ore c amount] / [iron ore a, b, c, d twenty quantities [iron ore D amount] /[Iron ore A, B, c, D^f ten amount]) • The average pore volume 铁 of the defined iron ore is 〇〇9cm3/g or less to match the sintering raw material of iron ore. Sinter. [2] In the above production method, the stone B is sintered in the raw material. [8] In the production method of the above [1], the sintered raw material is blended with iron ore 'stone A, iron ore b, and iron ore C. [8] In the manufacturing method of the above [2] or [3], the ratio of iron ore 6 to iron ore A, iron ore beta, iron ore c and iron ore]) is 20% by mass or more. The proportion of iron ore strontium is preferably 20 to 70% by mass, particularly 1 ΧΡ 2 ΧΡ / invention specification (supplement) / 94-12/94134179 1299363 is preferably 20 to 60% by mass. [5] In any one of the above [2] to [4], the ratio of iron ore D to the total amount of iron ore A, iron ore B, iron ore C, and iron ore D is 20 More than % by mass. The ratio of the iron ore D is preferably 20 to 60% by mass, and more preferably 20 to 50% by mass. Here, the average pore amount of the iron ore specified by the present invention is for the particle diameter of 4 to 7 mm. The average value of the micro-rude pores measured by the mercury intrusion measurement method (injection pressure: 0. 007 to 412 MPa) using a mercury intrusion type pore size measuring device (N=10 average value) Further, the above-mentioned pressing pressure range is a pressure at which the pore amount of the pore diameter of 0.035 to 200 //m can be measured, and by measuring in the pressure range, a usual mercury intrusion type pore distribution measuring device can be used. The fine pore amount of the iron ore A to C and the iron ore D of the object of the present invention is accurately measured. According to the present invention, the specific pore amount of the raw material ore which is incorporated in the sintering raw material is adjusted and the special phosphorus ore is considered. The specific average amount of porosity defined by the nature, regardless of the type of raw ore, can produce high quality Burning® ore; that is, even when combined with a considerable amount of high phosphate ore and/or Maramanba ore, High productivity and high finished product yield high cold room High-quality sintered ore. [Embodiment] It is explained that the iron ore (iron ore A to C) other than high-phosphorus ore is described. Figure 1 shows the manufacture of sintered ore using a real machine. In the test, change the blending ratio of Maramanba ore in the raw ore, investigate the production of sintered ore 312XP / invention manual (supplement) /94· 12/94134179 1299363: medium ^ horse; krf rate, " In this operation (3 days in the whole process), the ratio of raw ore 2, and the ore ore to the ore of ordinary ore is as shown in the figure 'Quality y: change for the following three levels: ( a) Hematite ore: 1〇〇20 shell hematite ore: (10) Please, Maramamba ore: granulation method and granulation conditions. The sintering raw materials belong to the mineral system. Also, the conditions of the red iron are ^1~(M°untNewman). Other manufacturing and operation Machine materials:: ratio of quicklime: 2·. · Sintering degree 580·, and, in addition, adjust the lime in the sintered raw material. Fineness I: Check the ratio of dolomite to make the sinter ore = amount%. 2Sl〇2. 5/1% by mass, CaO: 10.2 Qualitative f:%, MgO: 1. 〇: Figure, 1' with the proportion of the Maramanba ore in the raw ore two plus 'finished sintered stone The productivity and yield are reduced. For the reason, the result of the factory, 'can confirm that: if the proportion of the Maramanba ore is increased by ', then the strength of the sintering cooling room is reduced', which results in a decrease in productivity. In the manufacture, the H in the raw ore is operated at the following two levels: (4) Hematite of the fine powder: Ybori% other stone (general ore mainly composed of hematite ore): about 9〇 Quality m) Maramanba ore: about 1G f%, other ores (ordinary ore mainly composed of hematite ore): about 90% by mass, finished product 312XP / invention manual (supplement) / 94-12 /94134179 12 1299363 « Explosion # intensity] and productivity and other changes in the inspection of the grain ^ n in the general raw material in the vermiculite in the fine powder town (pill changed to the original =.:: two 1τ% of the sintering raw materials, = 1 « The granulation method is about 10 mass granulation granulation method (so-called qing method) red ^ sinter reinforced with raw materials. HPS method) granulation of sinter sintering raw materials to make the results according to Figure 3, relative to The raw material ore pellets) (she-, Yu; its::: cold strength-strength) is greatly reduced, a few It can be confirmed from the results of Fig. 3 and Fig. 3 that, irrespective of the granulation method or the conditions of the granulation, the cold strength of the finished sinter is blended with the Maramanba and the stone at a certain proportion. Will decrease. Here, it is known that the horse f ^ = ore is compared with other iron shirts, and the fine pores of the ore particles (four) are not suspended. It is considered that such fine pores existing inside the ore particles may affect the molten liquid formed during the sintering process. Behavior, which adversely affects the cold strength of the finished sinter. Therefore, the sintering raw material of the raw material ore shown in Table 1 was fired using the test apparatus shown in Fig. 4 having the test 〇〇 χ _ __) and the X-ray α device (sintering wind speed. 0. 29Nm) /s, coke ratio: 5, 5%, mixed raw material (five) ratio: 9. ^, mixed raw material Si〇4: 5.0%, raw material particle size: _3 leg), raw material ore and sintered cake stomata during sintering The structure and the turbid fluid flow condition 312XP / invention manual (supplement) / 94_ 12/94134179 1299363 for analysis. [Table 1 ]

Μ:貿恩特紐曼 *2 : MAC *3 :揚迪克吉那 ^此試驗中,針對以配合了表。.卜n〇 3之各原 =石的燒結簡,取得由燒結開始至燒結完了而經過— 二=後之料過程巾之原料❹及燒結餅的x射線 CT圖像。圖5中表示各燒結餅之χ射線CT圖像的一編 成完了後者)。根據此#x射線α圖像,以下述的手法这 打燒結中之各原料礦石及燒結餅的氣孔構造之解析與炫 融液流動狀態之解析。 於乳孔構造之解析中,如圖6所示般將乂射線^圖傳 二值化成固體部與氣孔部,再對此等進行細線化處理,由 此細線化處理圖像求出分枝(branch)(氣孔)之總面積 ymni2)與總長Lbt(mm),藉由分枝寬度=Ap/U)t求出分枝 寬度。此分枝寬度係相當於存在於燒結_内部的空洞大 /1、 〇 又,熔融液流動狀況之解析中,係如圖7所示般,將 隔開時間間隔的2個X射線α圖像(χ射線α圖像i=ti 秒’X射線CT圖像2=t2秒)二值化成為固體部與氣孔部, 根據此二值化圖像,求出在[t2_tl秒]間自固體部變化成 312XP/發明說明書(補件)/94·12/94134179 1299363 =部^面積S1、與同樣地由氣孔部變化成固體部的面 = = = 喷卿(㈣)求出炼融 :纟“虫液流動指數為在原料礦石粒子間的熔 W液的移動量(备i & pq ^母早位蚪間的移動量)之指標。 ㈣8表不燒結過程中之甩4 之解析結果。依此,二原 石及賴 礦石:60質量%)與N〇3(=f :4〇質量%、馬拉曼巴 皙旦G/W+人 ·(赤鐵礦· 40質量%、褐鐵礦:⑼ 車,與11(赤_:_質量%)的試驗例相 :即刀ί 成長速度與燒結餅的分枝寬度皆相當小。 10〇所二=Γ Ν〇·2與Ν〇·3的情況下,與Νο.1 (赤鐵礦: 00;f)相幸交,成長速度較慢,且氣孔不易變大。又,Μ: Traden Newman *2 : MAC *3 : Yan Dick Gina ^ In this test, the match was made to match the table. The original of the n = 3 = the sintering of the stone, the x-ray CT image of the raw material enamel and the sintered cake of the material process towel from the start of sintering to the completion of the sintering. Fig. 5 shows the completion of the latter of the x-ray CT image of each sintered cake. According to the #x ray α image, the analysis of the pore structure of each raw material ore and the sintered cake in the sintering and the analysis of the flow state of the blister were carried out by the following method. In the analysis of the milk hole structure, as shown in Fig. 6, the 乂 ray image is binarized into a solid portion and a vent portion, and then thinned, and the image is thinned to obtain a branch ( Branch) (the total area of the pores ymni2) and the total length Lbt (mm), the branch width is determined by the branch width = Ap / U)t. This branch width corresponds to the existence of the voids large/1, 〇 in the sintered_internal, and the analysis of the flow state of the melt, as shown in Fig. 7, two X-ray α images separated by time intervals (χ α α image i = ti seconds 'X-ray CT image 2 = t2 seconds) Binarization becomes a solid portion and a pore portion, and based on the binarized image, the solid portion is obtained between [t2_tl seconds] Change to 312XP/Invention Manual (Supplement)/94·12/94134179 1299363 = Partial area S1, and the surface which is changed from the pore portion to the solid portion in the same way = = = Spray ((4)) Find the refining: 纟" The flow index of the insect liquid is an index of the amount of movement of the molten W liquid between the raw ore particles (preparation of the amount of movement between the i & pq ^ mother early position). (4) The analytical result of 甩 4 in the process of 8 no sintering. Therefore, the two original stone and the Lai ore: 60% by mass) and N〇3 (=f: 4〇% by mass, Malamamba Badan G/W+ human (hematite 40% by mass, limonite: (9) In the test case of the car, 11 (Red _: _ mass %): the growth rate of the knife ί and the branch width of the sintered cake are quite small. 10 〇 2 = Γ Ν〇 · 2 and Ν〇 · 3 Next, with Ν .1 (hematite: 00; f) cross-phase Fortunately, slow growth, and the large pores and becomes difficult.

No 3(i:t . 40質量%、馬拉曼巴礦石:6。質量%)與 No. 3(赤鐵礦·· 4〇質晋%、说/ 較No ?夕“/ 鐵礦:60質量%)相較,No.3 較0.2之坎結餅的分枝寬度為大。 ::堯結過程中生成的氣孔,主要是因礦石粒子間的熔 融液私動而形成(亦即,炫 為氣孔),因而,分枝寬度的成的部分形成 t声夫f每力丄、+ 成長速度大且燒結餅的分枝 動;大。固9 A係思味著在礦石粒子間之熔融液的移 枝寬戶的m 數與根據圖8結果之分 枝=度的成長速度的關係,明白地顯示出上述 如上述,針_配合㈣石種類與其^ 之 相異㈣進行檢 存於礦石粒子原來所具有的微量二:大幅依 J12XP/翻說明書(補件)/94-12/94134179 15 1299363 以馬拉曼巴礦石與赤鐵礦礦石為例並依據圖10之示意圖 加以呪明,於圖10(a)所示之馬拉曼巴礦石的情況下,與 、,,礦礦石相較,由於在礦石粒子内部存在著非常多的微 、細氣孔,故於礦石粒子周圍生成的熔融液之相當量會被吸 收微細氣孔内,其結果,於礦石粒子間之熔融液的移 $里、交少。又,由於於燒結過程中生成的熔融液會成為結 •:礦石粒子間之黏合劑,若熔融液之相當量被吸收於微細 氣孔内則用以結合礦石粒子間的黏結劑的量不足,其結 •果會導致燒結礦的冷間強度降低。相對於此,於圖1〇(b) 所示之赤鐵礦礦石的情況下,由於礦石粒子内部的微細氣 孔幸乂 ^,在礦石粒子的周圍生成的熔融液之大部分不會被 及收到彳放細氣孔内而留在礦石粒子間,故於礦石粒子間之 熔融液的移動量會變多,其結果亦使氣孔變大。又,由於 留在此礦石粒子間的多量熔融液會成為使礦石粒子間結 合之黏合劑,故可得到冷間強度高的燒結礦。 φ 由以上的結果可知:欲提高成品燒結礦的冷間強度, 限制燒結原料中所配合之原料礦石的平均氣孔量係為有 效,不論礦石的種類,皆可得到具有既定水準以上之冷間 強度的成品燒結礦。因而,即使於多量配合馬拉曼巴礦石 的情形下,藉由適當地調整、選擇所配合之其他礦石的種 •類與其配合比例下,以限制原料礦石之平均氣孔量,則可 •得到冷間強度高的高品質成品燒結礦。 圖11為表示以水銀壓入測定法(用水銀壓入式細孔分 布測定裝置,於壓入壓力:〇·⑽7〜412Mpa下測定)測定之 312XP/發明說明書(補件)/94-12/94134179 16 1299363 赤^礦石、馬拉曼巴礦石及褐鐵礦礦石( 之礦石)之氣孔徑分布一例之曲線圖久強搜4〜7_ =樣=孔徑分布,根據該氣孔徑分布求 ,礦石除外)依對炫融液的行為上:’後述 W寡加以分類,可大致分為下述3種:。之化細氣孔 鐵礦石A平均氣孔量:0.03〜〇.〇5cmVg 鐵礦石B平均氣孔量:〇1〇〜〇12cm3/g 鐵礦石C平均氣孔量:〇.〇7〜〇.09cmVg 此處:鐵礦石A所包含之主要礦石可舉出 =鐵礦寻,又’鐵礦石B所包含之主要礦石可舉出:馬 又巴石廣石等;鐵礦石c所包含之主要礦石可舉出·以^石 :石為代表之褐鐵礦礦石等。用此3種類的鐵礦石A吒反 覆進行燒結試驗,得知:針對其等之微細氣孔量與 結鑛的冷㈣度之關加以整理之結果,在配合於燒結原= I的鐵礦石中,與熔融液的行為有關之鐵礦石的平均氣孔 里可用下式(a)定義,且藉由將此平均氣孔量χ定為 〇.〇9Cm3/g以下,可有效地提高成品燒結礦之冷間強度。 又,上述平均氣孔量為對粒徑4〜7mm的礦石,藉由使用水 銀壓入式細孔分布測定裝置之水銀壓入測定法(壓入壓 力·· 〇· 007〜412MPa)測得之微細氣孔量之平均值(N=1〇的 平均值)。 平均氣孔量 Χ=〇· 〇4χ[Α%] + 〇· 11χ[Β%] + 0· 〇8χ[α] ……(a) 312Xp/發明說明書(補件)/94-12/94134179 17 1299363 (其中, L:;丨.丨:礦石A*]/[鐵礦石A、B、C、D之合計量] 量]/[鐵礦石 A、B、C、k_]No 3 (i: t. 40% by mass, Maramamba ore: 6. Mass%) and No. 3 (hematite··4 〇 quality Jin%, said / No??) / Iron ore: 60 Compared with the mass %), the branch width of No.3 is larger than that of 0.2. The pores generated during the knotting process are mainly formed by the melt movement of the melt between the ore particles (ie, dazzle It is a pore), and thus, the portion of the branch width forms a t-fun f per force 丄, a growth rate of + is large and the branching of the sintered cake; a large solid 9 A system is thought of a melt between the ore particles. The relationship between the number of m of the branching households and the growth rate of the branching degree according to the result of Fig. 8 clearly shows that the above-mentioned needle-coordinating (four) stone types are different from those of the same (4) and are stored in the ore particles. The original traces of the two: according to J12XP / turn the instructions (supplement) / 94-12/94134179 15 1299363 Take the Malamamba ore and hematite ore as an example and according to the schematic diagram of Figure 10, in the figure In the case of the Maramamba ore shown in 10(a), compared with the ore, there are many micro and fine pores inside the ore particles. A considerable amount of the melt generated around the ore particles is absorbed into the fine pores, and as a result, the melt between the ore particles is shifted by a small amount, and the melt formed during the sintering process becomes a knot. : The binder between the ore particles, if the amount of the molten liquid is absorbed in the fine pores, the amount of the binder used to combine the ore particles is insufficient, and the result may cause the cold strength of the sintered ore to decrease. Therefore, in the case of the hematite ore shown in Fig. 1 (b), most of the molten liquid generated around the ore particles is not received and received due to the fine pores inside the ore particles. When the fine pores are left in the pores and remain between the ore particles, the amount of movement of the melt between the ore particles is increased, and as a result, the pores are enlarged. Further, since a large amount of molten liquid remaining between the ore particles becomes The binder is bonded between the ore particles, so that the sinter with high cold strength can be obtained. φ From the above results, it is known that the cold strength of the finished sinter is to be increased, and the raw ore to be blended in the sintered raw material is limited. The average pore volume is effective, and regardless of the type of ore, a finished sintered ore having a cold strength of more than a predetermined level can be obtained. Therefore, even in the case of a large amount of Maramanba ore, by appropriate adjustment and selection The ratio of the other ores of the other ore to the ratio of the average ore content of the raw ore can be used to obtain a high-quality finished sintered ore with high cold strength. Figure 11 shows the mercury intrusion measurement method. Mercury press-in type pore distribution measuring device, measured under pressure: 〇·(10)7~412Mpa) 312XP/invention specification (supplement)/94-12/94134179 16 1299363 red ore, malamamba ore And a plot of the pore size distribution of the limonite ore (the ore) is a long-term search 4~7_ = sample = pore size distribution, according to the pore size distribution, except for the ore) according to the behavior of the dazzling melt: 'described later W widows can be roughly classified into the following three types: Average pore volume of fine pore iron ore A: 0.03~〇.〇5cmVg Average ore content of iron ore B: 〇1〇~〇12cm3/g Iron ore C Average pore volume: 〇.〇7~〇.09cmVg Here: the main ore contained in iron ore A can be exemplified = iron ore, and the main ore contained in 'iron ore B can be exemplified by Ma Ba Ba Shi Guang Shi; the main part of iron ore c The ore may be a limonite ore represented by a stone: stone. The three types of iron ore A吒 were repeatedly subjected to a sintering test, and it was found that the iron ore was blended with the sintered original = I for the result of sorting the fine pore amount and the cold (four) degree of the ore. The average pore of the iron ore associated with the behavior of the melt can be defined by the following formula (a), and by setting the average pore volume to 〇.〇9 Cm3/g or less, the finished sintered ore can be effectively improved. The intensity of the cold. In addition, the average amount of pores is measured by a mercury intrusion measurement method (injection pressure·· 〇· 007 to 412 MPa) using a mercury intrusion pore size distribution measuring apparatus for ore having a particle diameter of 4 to 7 mm. The average of the amount of stomata (the average of N = 1 )). Average stomatal amount Χ=〇· 〇4χ[Α%] + 〇·11χ[Β%] + 0· 〇8χ[α] ......(a) 312Xp/invention manual (supplement)/94-12/94134179 17 1299363 (Where, L:;丨.丨: ore A*]/[total amount of iron ore A, B, C, D] Quantity]/[Iron ore A, B, C, k_]

又奸知:與斗八成 ,王J 礦石的-部份之丸粒礦料係使用作為燒結用原料 磁鐵礦,惟,由於料於礦!上係屬於赤鐵礦及 右私夫旦/鄉 、、〜、,故其微細氣孔對炼融液的行為 =i:r。因而於本發明中丸粒礦料被排除於鐵礦石Α 上述為配合鐵礦石a、b、c時之適當條件,而如下述 般,於配5向磷礦石時則有若干不同。 性::組::!?:、馬拉曼巴礦石,將其代表 質量減小(/、、,,σ日日水s有量之相關性高的加熱後 乂布:二r平:於表2 ’同樣地將代表性粒度構成(粒度 二Γ?)示於表3。依據此,高磷礦石的p 丨:旦:u廣石尚出甚多,相對於通常其他礦石的p含 !:為〇.06質量%以下’其含有0.10質量%以上的P。又, ㈣礦石之祕含有量較高,為2 G質量%以上,⑽雖 較褐鐵礦礦石為低’但為赤鐵礦礦石的約2倍。又〜 礦石的粒度構成之特徵為,粒徑㈣ ^ 為3職’與馬拉曼巴礦石-樣高,算 1.86_,為與馬拉曼巴礦石—樣的細粒。… 由上述之所謂高鱗礦石的特徵,可知高鱗礦石可由p 含有量與Ah〇3含量而與其他礦石(先前所列舉之鐵礦石 312XP/發明說明書(補件)/94-12/94134179 18 1299363 A〜C)區別出,因此,於本發明中,將P含有量:0. 10質 量%以上、Al2〇3含有量:2. 0質量%以上的礦石定義為「高 磷礦石」。And it is known that: with the Bachengcheng, Wang J ore - part of the pellets is used as a raw material for sintering magnetite, but, because of the mine! The upper system belongs to hematite and right private husband Dan / township, ~, so the behavior of its fine pores on the smelting fluid = i: r. Therefore, in the present invention, the pellets are excluded from the iron ore. The above-mentioned conditions are suitable for the combination of the iron ore a, b, and c, and there are some differences when the 5-way phosphate ore is used as described below. Sex:: Group::!?:, Maramamba ore, which is reduced in quality (/,,,, σ, daily water s, high correlation, high heating, 乂 cloth: two r flat: Table 2 'Similarly, the representative particle size composition (particle size Γ??) is shown in Table 3. According to this, the p 丨 of the high-phosphorus ore: Dan: u feldspar is still much, compared with the usual p ores of other ores!: It is 06.06 mass% or less 'it contains 0.10% by mass or more of P. Further, (4) the ore content of ore is relatively high, being 2 G mass% or more, and (10) being lower than limonite ore but being hematite The ore is about 2 times. The ~ ore particle size composition is characterized by the particle size (4) ^ for the 3 job 'with the Maramanba ore - the sample height is 1.86_, which is the fine grain with the Maramanba ore. From the characteristics of the above-mentioned so-called high-scale ore, it can be seen that the high-scale ore can be composed of p content and Ah〇3 content with other ores (previously listed iron ore 312XP/invention specification (supplement)/94-12/ 94134179 18 1299363 A to C) are distinguished. Therefore, in the present invention, the P content is: 0.1% by mass or more, and the Al2〇3 content: 2.0% by mass or more of ore is defined as " High phosphate ore."

312XP/發明說明書(補件)/94-12/94134179 19 1299363 i 1ΌΙ *6 (質1» 4 40 ai 10· 40 1.54 LO τ—1 od 〇 1—Η 寸· 化學組成(質1%) T-H CD r—Η 〇· 0.00 τ—Η CD CD CD CD CD τ·—H czi τ· η, < CD 1—Η CD 1 < CZ5 g pL-ι 0.47 0.10 0.14 0.27 0.93 r—Η CO 0.033 0.014 0.015 0.002 0.005 0.008 Oh 0.123 0.041 0.036 0.024 0.039 0.052 A1A CO T—H 03 oi OO oo r—H 0.60 1.36 2.03 cS 00 3.47 5.52 oo CX) 寸· 3.11 2.68 CO CO T.Fe 62.70 57.11 58.33 66.60 66.35 62.32 ψ 南石粦石廣石 梅載礦(1) *1 褐鐵瞻(2)柁 南美產赤4載礦礦石*3 澳洲產赤鐵礦礦石*4 馬拉曼巴礦石*5 s ¥虑*囊 9* 9* s* I* 6卜 i 寸e i 寸6/π46/ffsi)_s?iis餾/dxn ε 1299363 1 1 iNi(im) 1.86 CO r—H CO CO 2.66 3.36 1.96 ψ\ 麵c 衾 -0.125mm 〇〇 1 < CO CO CNJ CQ CJD r—H LO CNJ +0· 125mm LO T—H CJD CO 卜 寸 +0.25mm CO r-H CO r-H 0 T—< CO CO +0.5mm r-H 1 < D— r—H r-H 00 00 τ—Η +1刪 00 t—H LO oa 00 oa CH) t—< 贫 r-H r-H +3imi CO t—H CO r—H 00 t—H CO τ—Η 卜 +5nm t—H r—H CO r—H CO r-H r—H CH) +8mn r-H CD 00 CNI 卜 CO +10nm CD 寸 卜 1—H CO CO .Aftiij ψ 向石粦石廣石 < /^N r-H 赛 褐鐵礦(2)柁 南美產赤4載礦礦石*3 澳洲產赤鐵礦礦石*4 馬拉曼巴礦石*5 9兴 Co* ¾3 I*312XP/Invention Manual (supplement)/94-12/94134179 19 1299363 i 1ΌΙ *6 (Quality 1» 4 40 ai 10· 40 1.54 LO τ—1 od 〇1—Η inch · Chemical composition (quality 1%) TH CD r—Η 〇· 0.00 τ—Η CD CD CD CD CD τ·—H czi τ· η, < CD 1—Η CD 1 < CZ5 g pL-ι 0.47 0.10 0.14 0.27 0.93 r—Η CO 0.033 0.014 0.015 0.002 0.005 0.008 Oh 0.123 0.041 0.036 0.024 0.039 0.052 A1A CO T—H 03 oi OO oo r—H 0.60 1.36 2.03 cS 00 3.47 5.52 oo CX) Inch · 3.11 2.68 CO CO T.Fe 62.70 57.11 58.33 66.60 66.35 62.32 ψ South Shijieshi Guangshimei Loading Mine (1) *1 Brown Iron Prospect (2) Minnan American Red 4 ore *3 Australian Hematite Ore*4 Malamamba Ore*5 s ¥**9* 9* s* I* 6 ii i inch ei inch 6/π46/ffsi)_s?iis distillation/dxn ε 1299363 1 1 iNi(im) 1.86 CO r-H CO CO 2.66 3.36 1.96 ψ\ face c 衾-0.125mm 〇〇1 < CO CO CNJ CQ CJD r-H LO CNJ +0· 125mm LO T-H CJD CO Bu inch +0.25mm CO rH CO rH 0 T—< CO CO +0.5mm rH 1 < D— r—H rH 00 00 τ—Η +1 00 00 t—H LO oa 00 oa CH) t—< rH rH +3imi CO t—H CO r—H 00 t—H CO τ—Η Bu+5nm t—H r—H CO r—H CO rH r—H CH) +8mn rH CD 00 CNI Bu CO +10nm CD inch 1-H CO CO .Aftiij ψ 粦 石粦石广石< /^N rH 赛红铁矿(2) 柁南美产赤四载矿 ore*3 Australian hematite ore*4 Malaman巴矿石*5 9兴Co* 3⁄43 I*

I 6卜 I 寸ε I 寸6/3 r寸 6/ff}ffi)_^?is^/dxrNll e 1299363 %:::=石::=石(,5"量 質量比例與化學組& ° /石4Q貝量%)之每粒度的 〇. 063_以下二 IV依此’高鱗鑛石中粒徑 祕含有旦二 例夕達24質量%,且其微粉中之I 6 I I inch ε I inch 6/3 r inch 6/ff}ffi)_^?is^/dxrNll e 1299363 %:::=石::=石(,5"quantity mass ratio with chemical group & ° / stone 4Q shell amount %) of each particle size . 063_ below two IV according to this 'high-scale ore particle size secret contains two cases of eve up to 24% by mass, and its fine powder

Ai2〇3;:;:;^ 原二表石4 ?〇. 1〜N〇, 3所表示之褐鐵礦礦石1 °°質細 配合於燒結中石取代之原料㈣ X : 3〇〇"Φ 衣ι此丨月形下之原料裝填密 ;二!! 中風速及燒結時間示於圖13。其他的 兀、、、“木件疋為吸引壓力:i〇〇〇_h2〇,焦炭比:5 3%、混 =枓中ca0比:9%、混合原料中Si〇2比:5%、原料粒度: 。得到之成品燒結礦的品質、生產率及產率示於圖 籲[表4]Ai2〇3;:;:;^ The original two stones 4 ?〇. 1~N〇, 3 represents the limonite ore 1 ° ° fine texture combined with the raw material replaced by the sintered stone (4) X : 3〇〇" Φ ι ι This month's raw materials are packed tightly; Second!! The mid-speed and sintering time are shown in Figure 13. Other 兀,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,,, Raw material particle size: The quality, productivity and yield of the finished sinter obtained are shown in Figure [Table 4]

No. 高磷礦石 褐鐵礦礦石(2) 1 - 100質量% 2 冗》量% 70質量% 3 60質量% —-—-__ 40質量% 依據圖13 ’隨著相對於No· 1的褐鐵礦礦石i 〇〇質量% 增加高磷礦石配合量(取代量)(Ν〇· 2 + Ν〇· 3),由於係以比 重i且粗粒之褐鐵礦礦石進行取代,故裝入容積密度增 加,同時假粒徑降低。又,隨著高磷礦石配合量之增加, 312XP/發明說明書(補件)/94-12/94134179 22 !299363 燒結中之風速(通氣性)會降低,燒結時間變長。又佑 圖14,儘管增加高磷礦石的配合量,而以 所、據 、载j礦石予以取代,成品燒結礦的生產率與產率亦降低。 具體而言,將高磷礦石每以丨〇質量%之褐鐵礦礦石予以取 代,生產率會降低〇.〇lt/hr · m2。就其理由進行查察之姓 確認得知:高磷礦石的配合量若增加,燒結礦:冷: 3度T降低,其結果會導致成品產率與生產率降低。再 者L隨著高磷礦石的配合量增加,被還原性雖變化 但還原粉化性變差。 圖15為配合了褐鐵礦礦石1〇〇質量%之燒結原料(表4 所旦:.1)、與配合了高鱗礦石60質量%、褐鐵礦礦石40 G ^ 表4之N Q ·3)之上述燒結試驗中,就燒 ',、。中的通氣性變化進行查察者。依此可知:相對於N 〇 i 褐鐵礦礦石1〇〇質量%之燒結原料,以相當量配 變=戶、石之No. 3的燒結原料的燒結時間變長,通氣性 化,:二入右’主目於燒結過程中之通氣性(氣體風速)的變 :氣力:Γ廣石之燒結原料中,於主要爾 特別3 + 的&、、、°别+部中,其通氣性變差,而 中,γ、ρ要炫融帶下之通氣阻力為支配性的燒結後半部 性惡化的影響為:由廣… 由造粒之假粒徑不^么廣石為細粒,故造粒性降低(經 w的通氣性變差,但其影響小;另一方面,於主要高鱗 3】2XP/發明說明書(補件购2/94134179 23 !299363 顯著,此對冷間強 礦石熔融狀態(熔融帶)下之通氣性惡化 度與生產性有重大的不良影響。 成=她與圖15同樣的燒結原料燒成時之排氣組 仃一祭之結果。依此,相對於、、’ 石雇石1 η η #曰。 · 1之配合了褐鐵礦 Ν:二貝!%的燒綱’配合了高鱗礦;Μ目當量之'、 • 3的k結原料的排氣中之C0濃度上昇 1 to丄I 反上汁,C〇2濃度降低。 :由在於隨著高磷礦石之配合而焦炭的燃燒性被阻礙 稻角等曾有報告指出:熔融液的流動性若變 差,則焦厌被熔融液包圍住而進行燃燒的比例增高,其結 果,會阻礙焦炭之燃燒性(鐵與鋼,vol.78 (1 99 /、、° P· 1 053) 〇 ’ 上述之通氣性惡化(圖15)與焦炭燃燒性惡化(圖丨〇之 原因,據推測係因高磷礦石之配合導致燒成時之熔融液流 動性降低之故。本發明者等,著眼於先前舉出之高磷礦石 的成分組成及粒度構成上的特徵,亦即,著眼於微粉的比 φ例多且在此微粉中之Al2〇3含有量非常高之特徵,而推測 認為··作為熔融液生成的基點且為熔融液生成來源的主要 部分之微粉中含有多量的Al2〇3,為配合有高磷礦石之情 形下之導致纟谷融液流動性變差的原因,為了確認此論點, 係進行了下述實驗。 ,於CaO : 20質量%、Fe2〇3 : 80質量%之CaO-Fe2〇3系熔融 液中,分別以〇· 5質量%、1質量%、2質量。/。、6質量%、8 質量%的比例添加Al2〇3試藥,測定於l30〇°c、1350°c、14〇〇 °C各溫度之各熔融液的黏度。 24 312XP/發明說明書(補件)/94·12/94134179 1299363 ^,通常,130(TC相當於燒結床之上層溫度,14〇〇它 相虽於燒結床之下層溫度。此溶融液之黏度測定係採用圖 • Η所不的球拉上法。此測定方法,係依據於將吊下至熔 .融液中的球拉上時天平指針在區間之移動速度來算 出黏,三圖18表示其結果,可知:與熔融液的溫度無補 地,隨著Al2〇3添加量增大,熔融液的黏度也上昇。 ★然後,使用上述試驗中顯示各種黏度之熔融液,測定 鲁此等炫融液於填充層中之浸透速度,調纽融液的黏度與 填充層中之熔融液的浸透速度之關係。此浸透速度之測定 係用f 19所示的浸透試驗裝置。此試驗裝置,係於縱長 的圓筒容器内形成玻璃珠之填充層’自此填充層上部滴下 溶融液而測定熔融液於填充層内之浸透速度。圖20為根 據測得之熔融液之浸透速度而顯示熔融液的黏度與浸透 速度之關係者’可知:熔融液的黏度上昇之同時,熔融液 的/又透速度(流動性)下降。 • 由以上之結果可推斷:於高磷礦石的情形下,由於因 A 12〇3合有濃化之多量的微粉所致,熔融液黏度變大之故, 使得炫融液之流動性降低(亦即,於礦石粒子間之炫融液 的移動量減少),阻礙燒結餅中之氣孔的成長,因此而導 致通氣!·生又差與焦炭燃燒性惡化,而使得成品燒結鑛之冷 ,間強度降低與生產率、產率降低。 口而-於配合兩磷礦石時之配合條件,除了須與鐵礦 f A〜C同樣地考慮前述之平均氣孔量對於冷間強度的影 曰卜亦須考慮因微粉(A12〇3濃化之微粉)所致之溶融液 312XP/發明說明書(補件)/9(12/94134179 25 1299363 _動性降低所引起的冷間強度降低等。 入百先,藉由與圖11同樣的水銀壓入測定法(用水銀壓 、j細孔分布測定裝置,於壓入壓力:0 007〜412M阳下 ::)就高磷礦石之氣孔徑分布加以查察,依據該氣孔徑 ::未出加重平均氣孔量之結果,得知;高磷礦石(鐵礦 旦之平均氣孔量(與熔融液的行為有相關性之微細 I)為下述之範圍内。 • 鐵礦石D平均氣孔量·· 〇.〇5〜〇 〇7cmVg 又’用此高填石廣石(鐵礦石D)與上述3種類的鐵礦石 的牲2進行燒結試驗’對上述般的高磷礦石(鐵礦石D) 究之外’並對其等之微細氣孔量與成品燒 冷間強度的關係加以整理之結果,得知:於配 ::=鐵:廣石_情形下,與炫融液的行為有相關性: = 氣孔量可用下述式⑴定義,且藉由 ,孔1 X定為,可有效 由使用水㈣人式細孔分布㈣裝置之水 測疋法(壓入壓力:0.00wl2Mpa)測得之 均值(N=l〇的平均值) 、,矾孔里之平 ^均氣孔量 X--0.04x u%]+011 x [叫 [C/〇]i2. Ο x 0. 06 X [D%] , r甘由 」 ……式⑴ (其中, β之合計量] D之合計量] [A%] ··[鐵礦石A量]/[鐵礦石Α、β、c [B%] ··[鐵礦石β量]/[鐵礦石A、β、c 3】2ΧΡ/發明說明書(補件)/94-12/94】34179 26 1299363 [c%]:[鐵礦石c量]/[鐵礦石Α、β、c、D之人叶 [W:[鐵礦石D量]/[鐵礦石a、b、c、d之:計 圖21係將上述試驗之結果整理者,顯*燒結原料中所 配合之鐵礦石(包含高磷礦石之鐵礦石)的平均氣孔量 1(二述式⑴定義之平均氣孔量x)與成品燒結礦的冷間 強度(shutter強度)之關係。如同圖所示般可知:藉 燒結原料中所配合的鐵礦石之平均氣孔量X定為 dVg以下’可使成品燒結礦的冷間強度(shutter強 度)在管理值89.5%以上的水準。平均氣孔量χ尤以 〇· 04〜0· 08cm3/g 為佳。 因而,於本發明中’係由作為原料礦石之至少一部份 述鐵礦石A〜c中之至少2種的鐵礦石、與鐵礦石 =石只石)配合成之燒結原料製造燒結石廣時,使於燒結 0〇q ^以上述式⑴定義的鐵礦石之平均氣孔量X成為 石廣。CD1⑼下而配合鐵礦石’再由此燒結原料製造燒結 屬^1 之本發明之燒結礦的製造方法,於配合相當量的 it又巴礦石之鐵礦石B、與高鱗石廣石之鐵礦石_ 二寺別有用’例如,⑴對鐵礦石A、鐵礦石B、鐵礦 :鐵礦石D之合計量(其係包含未配合人鐵礦石a〜c 上壬—者的情形)的鐵礦石B之配合比例為2〇 f量0/〇以 鐵配合量配合鐵礦石㈣情形;(2)對鐵礦石A、 入^ 鐵礦石C、冑礦石D之合計量(其係包含未配合 。K石A C中之任一者的情形)的鐵礦石D之配合比例 XP/發明說鴨(翻12/94134179 27 1299363 為20質量%以上之以高配合量配合鐵礦石D的情形;(” 對鐵礦石A、鐵礦石B、鐵礦石c、鐵礦石邛之合計量(其 係包含未配合人鐵鑛石K中之任—者的㈣/的鐵 itr合比例為2G質量%以上、鐵礦石D之配合比例為2〇 貝1 %以上之以同配合量配合鐵礦石B、鐵福石D的情形 等’即使於此等情形中亦可製得在高成品產率與高生產率 下製造冷間強度高的高品質燒結礦。 【圖式簡單說明】 圖1為表示原料礦石中之馬拉曼巴礦石的配合比例與 成品燒結礦的生產率及產率之關係的曲線圖。 、 圖2為表示圖1的試驗中原料礦石之配合比例的說明 圖。 圖3表示針對燒結原料中配合了微粉礦石+普通礦石的 刼作例、與配合了馬拉曼巴礦石+普通礦石之操作例,焦 炭比及燒結礦的冷間強度變化之曲線圖。 圖4表示用於進行燒成中的原料礦石及燒結餅的氣孔 構造與溶融液流動狀況之解析所用之試驗裝置的說明圖。 圖5表示以圖4的試驗裝置得到的燒結餅之X射線CT 圖像之一例的圖式。 圖6為表不用於進行燒成中的原料礦石及燒結餅的氣 孔構造之解析所採取的手法之說明圖。 圖7為表不用於進行燒結中的原料礦石及燒結餅的熔 融液流動之解析所採取的手法之說明圖。 圖8為表示燒成中之原料礦石及燒結餅之分枝(氣孔) 312XP/發明說明書(補件)/94·〗2/94〗^ 28 1299363 寬度的變化之曲線圖。 圖9為圖8所得之分枝寬度 指數之關係的曲線圓。 長速度與熔融液流動 圖1 〇(a)、(b)為針對燒結過程中生 1拉Λ巴^與赤鐵石廣石為例而表示之行為, 圖11為表示以水銀麗入法測定 石廣石及褐鐵礦石之氣孔徑分布之一例的曲線圖。馬拉又巴 圖12表示高磷礦石與摻合礦石 旦 學組成的曲線圖。 八 才' 度的貝夏比例與化 圖13為表示將表4的N〇 1〜N 於房料中田迠从 .No. 3的原料礦石分別配合 行燒結石廣之製造時之原料 衣:徑、燒結中風速及燒結時間之曲線圖: 於二々料:不::4的N。·1〜N。· 3的原料礦石分別配合 產燒結試驗銷所製造之燒結礦的品質、生 產率及產率之曲線圖。 王 圖15為表示分別配合了表4的No. i與Νο. 3之原料礦 石之燒結原料中,苴燒姓中 ” 4廣 、、"之通氣性的變化之曲線圖。 圖16為表示將分別配合了表4的版 礦石门之燒結原料,進行燒成時的排氣組成之曲線圖 圖圖Π表祕融液之黏度測定所用的球拉上法之說明 二 …1 203試藥的⑽,203編 4占度之曲線圖。 圖19表示用以測定在炫融液的填充層中之浸透速度的 312XP/發明說明書(補件)/94-12/94134179 29 1299363 裝置之說明圖。 圖20為表示熔融液之黏度與填充層中之浸透速度的關 係之曲線圖。 圖21為表示配合於燒結原料中之鐵礦石的平均氣孔量 X與成品燒結礦之冷間強度(shut ter強度)的關係之曲線 圖0No. High phosphate ore limonite ore (2) 1 - 100% by mass 2 Redundant amount % 70% by mass 3 60% by mass —---__ 40% by mass According to Fig. 13 'With brown relative to No. 1 Iron ore ore i 〇〇 mass % increase the amount of high-phosphorus ore (substitution amount) (Ν〇 · 2 + Ν〇 · 3), because it is replaced by a specific gravity i and coarse-grained limonite ore, so the volume The density increases while the false particle size decreases. Also, with the increase in the amount of high-phosphorus ore, the 312XP/invention specification (supplement)/94-12/94134179 22 !299363 will reduce the wind speed (ventilation) during sintering and the sintering time will become longer. Also, Figure 14. Although the addition of high-phosphorus ore is increased, it is replaced by the ore, and the productivity and yield of the finished sinter are also reduced. Specifically, the high-phosphorus ore is replaced by the limonite ore of 丨〇% by mass, and the productivity is lowered by 〇.〇lt/hr·m2. The surname for the reason for the inspection confirmed that if the amount of high-phosphorus ore is increased, the sinter: cold: 3 degrees T decreases, which results in a decrease in the yield and productivity of the finished product. Further, as the amount of the high-phosphorus ore is increased, the reduction property is changed, but the reduction powdering property is deteriorated. Figure 15 is a sintered raw material with 1% by mass of limonite ore (Table 4: 1.1), 60% by mass with high-grade ore, 40 G ^ for limonite ore, NQ · 3 In the above sintering test, it burns. The change in ventilation is carried out by the inspector. According to this, it is known that the sintering time of the sintering raw material of the N 〇i limonite ore is 1% by mass, and the sintering time of the sintering raw material of No. 3 of the household and the stone is longer, and the air permeability is improved. The change in the air permeability (gas wind speed) in the sintering process is: the gas force: in the sintering raw material of the Γ广石, the venting property is changed in the main 3 + & The difference between γ and ρ is to dominate the venting resistance under the smelting zone. The effect of the deterioration of the semi-sintering after sintering is: from the wide... The granulated pseudo-particle size is not fine, the feldspar is fine, so granulation Reduced (the aeration of w is worse, but its effect is small; on the other hand, in the main high scale 3) 2XP / invention manual (replacement purchase 2/94134179 23 !299363 significant, this pair of cold strong ore molten state The degree of deterioration of the air permeability under the (melting zone) has a significant adverse effect on productivity. Cheng = the result of the exhaust group of the same sintering material as that of Fig. 15 when it is fired. Stone hired stone 1 η η #曰. · 1 with the limonite Ν: two shells!% of the burnt 'coordinated with high-scale ore; ', • The concentration of C0 in the exhaust gas of the k-knot material is increased by 1 to 丄I, and the concentration of C〇2 is lowered. The burning property of coke is hindered by the combination of high-phosphorus ore. It has been reported that if the fluidity of the melt deteriorates, the proportion of burnt gas surrounded by the melt is increased, and as a result, the combustion of coke is hindered (iron and steel, vol.78 (1 99 / , ° P· 1 053) 〇' The deterioration of the above-mentioned air permeability (Fig. 15) and the deterioration of coke flammability (the reason for the figure is that the fluidity of the melt at the time of firing is lowered due to the combination of high phosphate ore. The inventors of the present invention have focused on the composition and particle size composition of the previously-expressed high-phosphorus ore, that is, the ratio of the fine powder to the φ is large and the Al2〇3 content in the fine powder is very high. It is presumed that the fine powder which is the main part of the source of the melt is contained in the fine powder which is the base of the melt and contains a large amount of Al2〇3, which causes the flow of the glutinous rice melt in the case of the high phosphate ore. The reason for the poor sex, in order to confirm this argument, The following experiment was carried out: in a CaO-Fe2〇3-based melt having CaO: 20% by mass and Fe2〇3: 80% by mass, respectively, 5% by mass, 1% by mass, and 2% by mass. The Al2〇3 reagent was added in a ratio of 6 mass% to 8 mass%, and the viscosity of each melt at each temperature of l30〇°c, 1350°c, and 14〇〇°C was measured. 24 312XP/Invention Manual (Supplement) /94·12/94134179 1299363 ^, usually, 130 (TC is equivalent to the upper layer temperature of the sintering bed, 14 〇〇 is the temperature below the sintering bed. The viscosity of the molten solution is determined by the ball Pull the law. This measurement method is based on the moving speed of the balance pointer in the section when the ball suspended from the melt and melt is pulled up. The result is shown in Fig. 18, and it is known that the temperature of the melt is not compensated. The amount of addition of Al2〇3 increases, and the viscosity of the melt also rises. ★ Then, using the melts showing various viscosities in the above test, the soaking speed of the smelting liquid in the packed bed was measured, and the relationship between the viscosity of the melting liquid and the immersion speed of the molten liquid in the packed bed was measured. The soaking speed was measured by the soaking test apparatus shown by f19. In this test apparatus, a filling layer of glass beads was formed in a vertically long cylindrical container. The molten solution was dropped from the upper portion of the packed bed to measure the rate of penetration of the molten metal in the packed bed. Fig. 20 is a graph showing the relationship between the viscosity of the melt and the permeation rate based on the measured impregnation speed of the melt. It is understood that the viscosity of the melt increases and the flow rate (fluidity) of the melt decreases. • From the above results, it can be inferred that in the case of high-phosphorus ore, the fluidity of the molten liquor is lowered due to the increased viscosity of the melt due to the concentration of fine powder of A 12〇3. That is, the amount of movement of the turbid liquid between the ore particles is reduced, which hinders the growth of the pores in the sintered cake, thereby causing ventilation; the poor quality of the raw coke and the deterioration of the coke combustion, and the cold of the finished sinter, The strength is lowered and the productivity and the yield are lowered. In addition to the iron ore f A to C, the above-mentioned average pore volume should be considered in addition to the iron ore f A to C. The effect on the intercooling strength must also be considered due to the fine powder (A12〇3 concentrated Melting solution 312XP/invention manual (supplement)/9 (12/94134179 25 1299363 _ reduction in cold strength caused by lowering the dynamics, etc. into the first, with the same mercury intrusion as in Fig. 11 Determination method (silver pressure, j pore distribution measuring device, under pressure: 0 007~412M cation::) to check the pore size distribution of high phosphate ore, according to the pore diameter:: no weighting average As a result of the amount of pores, it is known that high-phosphorus ore (the average pore volume of iron ore (fine I related to the behavior of the melt) is within the following range. • Average ore content of iron ore D·· 〇 .〇5~〇〇7cmVg and 'Sintering test with this high-filled feldspar (iron ore D) and the above three types of iron ore 2' to the above-mentioned high-phosphorus ore (iron ore D) In addition to the results of the relationship between the amount of fine pores and the strength of the finished product, it is known that: With::=Iron:Guangshi_In case, it has a correlation with the behavior of the squirting liquid: = The amount of stomata can be defined by the following formula (1), and by using the hole 1 X, it can be effectively used by the water (4) Hole distribution (4) The mean value of the water measurement method (injection pressure: 0.00wl2Mpa) (the average value of N=l〇), and the average pore volume in the pupil X--0.04xu%]+011 x [called [C/〇]i2. Ο x 0. 06 X [D%] , r 甘由" ...... (1) (wherein the total amount of β is the sum of D) [A%] ··[Iron Ores A amount] / [iron ore Α, β, c [B%] · [[iron ore beta amount] / [iron ore A, β, c 3] 2 ΧΡ / invention manual (supplement) / 94 -12/94】34179 26 1299363 [c%]: [Iron ore c amount] / [Iron ore, β, c, D of human leaves [W: [iron ore D amount] / [iron ore a, b, c, d: Figure 21 is the result of the above test, the average porosity of iron ore (including iron ore with high phosphate ore) in the sintered raw material is 1 (two The relationship between the average pore volume x) defined by the formula (1) and the cold strength (shutter strength) of the finished sintered ore. As shown in the figure, it is known that the iron ore blended in the sintered raw material The average stomatal amount X of the stone is set to be below dVg, so that the cold strength (shutter strength) of the finished sinter can be above the management value of 89.5%. The average stomatal amount is preferably 〇·04~0·08cm3/g. Therefore, in the present invention, 'made of a sintered raw material which is synthesized from iron ore of at least two kinds of iron ore A to c which is at least a part of raw ore, and iron ore = stone stone) When the sintered stone is wide, the average pore amount X of the iron ore defined by the above formula (1) at the time of sintering is 石石广. CD1(9) is combined with iron ore' to produce a sintered ore according to the present invention from the sintered raw material, and is combined with a considerable amount of iron ore B of the itba ore and iron of the high-scale stone Ore _ two temples are useful 'for example, (1) for iron ore A, iron ore B, iron ore: iron ore D total (which includes unmatched human iron ore a~c upper 壬 - The case ratio of iron ore B is 2〇f amount 0/〇 with iron compounding amount in combination with iron ore (4); (2) total for iron ore A, iron ore C, and antimony ore D The ratio of the iron ore D of the amount (which is not included in the case of any of K-stone AC) XP/invention said that the duck (turning 12/94134179 27 1299363 is 20% by mass or more with a high blending amount) The case of iron ore D; (" the total measurement of iron ore A, iron ore B, iron ore c, iron ore ( (which includes the unmatched human iron ore K) / The ratio of iron itr is 2G mass% or more, and the blending ratio of iron ore D is 2 mutex or more, and the amount of iron ore B and iron sulphate D is blended with the same amount, etc. In the form, high-quality sintered ore with high cold strength can be produced under high yield and high productivity. [Simplified Schematic] Figure 1 shows the blending ratio of the Maramanba ore in the raw ore and the finished product. Figure 2 is a graph showing the relationship between the productivity of the sintered ore and the yield. Fig. 2 is an explanatory view showing the mixing ratio of the raw ore in the test of Fig. 1. Fig. 3 is a view showing an example of a mixture of fine ore or ordinary ore in the sintered raw material. A graph showing the coke ratio and the change in the cold strength of the sintered ore with the operation example of the Malamamba ore + ordinary ore. Fig. 4 shows the pore structure and molten solution for the raw ore and the sintered cake in the firing. Fig. 5 is a view showing an example of an X-ray CT image of the sintered cake obtained by the test apparatus of Fig. 4. Fig. 6 is a view showing the raw material ore used for the firing. And the explanation of the method used for the analysis of the pore structure of the sintered cake. Fig. 7 is a diagram showing the method used to analyze the flow of the raw material ore and the molten cake in the sintering. Fig. 8 is a graph showing the variation of the width of the raw material ore and the sintered cake in the firing (stomach) 312XP/invention specification (supplement)/94·〗 2/94〗 28 2899363. The curve of the relationship between the branch width index obtained in Fig. 8. Long velocity and melt flow Figure 1 〇(a), (b) is an example of the production of Λ拉巴 and Hematite feldspar during the sintering process. Behavior, Fig. 11 is a graph showing an example of the pore size distribution of Shiguangshi and limonite ore by the mercury glazing method. Mara Batu 12 shows a graph of the composition of the high phosphate ore and the blended ore. Fig. 13 shows the ratio of N〇1 to N in Table 4 to the raw materials of the raw material ore from No. 3 in the material. Curve of sintering mid-wind speed and sintering time: in two materials: not:: 4 N. · 1~N. · The raw material ore of 3 is matched with the graph of the quality, productivity and yield of the sintered ore produced by the sintering test pin. Fig. 15 is a graph showing the change in the air permeability of "4 Guang," " in the sintered raw material of No. i and Νο. 3 of Table 4, respectively. The graph of the composition of the exhaust gas at the time of firing is prepared by the sintering raw materials of the ore gate of Table 4, respectively. The description of the ball pull method used for the measurement of the viscosity of the secret melt is shown in Fig. 2... (10), 203 is a graph of 4 degrees of occupation. Fig. 19 is an explanatory view showing a device for measuring the penetration speed in the packed layer of the shale liquid, 312XP/invention specification (supplement)/94-12/94134179 29 1299363. Figure 20 is a graph showing the relationship between the viscosity of the melt and the penetration speed in the packed bed. Figure 21 is a graph showing the average pore volume X of the iron ore blended in the sintered raw material and the cold strength of the finished sintered ore (shut ter) Curve of the relationship of strength)

312XP/發明說明書(補件)/94-12/94134179 30312XP/Invention Manual (supplement)/94-12/94134179 30

Claims (1)

1299363 十、申請專利範圍·· 1.—種燒結礦之製造方法,係由配合了作為 :至^ ’份之選自··鐵礦石A,係以水銀壓入測定、、: 定之平均氣孔量為0.03〜0.05cmVg(其中,丸粒礦料〜 =i et f eed)除外),·鐵礦石B,係同上之平均氣孔量為 〜0.i2cm3/g;鐵礦石c,係同上之平均氣孔量為— 0. 07〜〇. 〇9Cm3/g;中之至少2種的鐵礦石(其中,鐵礦石A、 B、C為排除p含有量為〇1〇質量%以上且Ai2〇3含有 =〇^量%以上者)、與P含有量為〇1〇質量%以上且Ah〇3 含有置為2.0質量%以上之鐵礦石D之燒結原料製造燒結 礦者;其特徵在於, ° 以由下述式(1 ): Ψ 平均氣孔量 X = 0.04 X [Α%]+0·11 X [Β%]+〇·〇8 X [C%]+2.〇 χ 0.06 χ [D〇/〇] ······式⑴ (其中, [7] •[鐵礦石A量]/[鐵礦石A、B、C、D之合計量] [抓]·[鐵礦石B量]/[鐵礦石A、B、C、D之合計量] [C/g ][鐵礦石C量]/ [鐵礦石a、b、C、D之合計量] [W、:[鐵礦石D量]/[鐵礦石A、B、C、D之合計量]) 所定義之鐵礦石的平均氣孔量X成為〇 〇9cmVg以下之方 式,由配合了鐵碌石之燒結原料製造燒結礦。 2·如申睛專利範圍第1項之燒結礦之製造方法,其中, 燒結原料中係配合鐵礦石B。 3·如申請專利範圍第1項之燒結礦之製造方法,其中, 312XP/發明說明書(補件)脉丨2/9413川9 ^299363 燒結原料φ # 4如 τ'配合鐵礦石A、鐵礦石β及鐵礦石c。 鐵一二專:二圍第2項之燒結礦之製造方法,其中, 人舛θ 戥礦石Α、鐵礦石Β、鐵礦石C及鐵礦石 …之比例為20質量%以上。 W石D的 .如申凊專利範圍第2項之燒 鐵礦石D對钙成r Λ 檢之製造方法,其中, 對鐵礦石A、鐵礦石Β、鐵礦石Γ穷朽戚^ n 合計量之比例為2〇質量%以上。及鐵礦石D的1299363 X. Scope of application for patents·· 1. A method for producing sinter ore, which is selected from: to ^' parts selected from · · iron ore A, measured by mercury intrusion, and: average vent The amount is 0.03~0.05cmVg (except for the pellet minerals ~ = i et f eed), · · Iron ore B, the average stomatal amount is the same as above ~0.i2cm3 / g; iron ore c, the same as above The average amount of pores is -0. 07~〇. 〇9Cm3/g; at least two kinds of iron ore (wherein iron ore A, B, and C are excluded from p content of 〇1〇% by mass or more Ai2〇3 contains 〇 以上 量 ) 、 、 、 ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; ; Therefore, ° is given by the following formula (1): Ψ Average pore volume X = 0.04 X [Α%]+0·11 X [Β%]+〇·〇8 X [C%]+2.〇χ 0.06 χ [D〇/〇] ·······(1) (Where, [7] • [Iron ore A amount] / [Iron ore A, B, C, D total measurement] [Catch]·[Iron Ore B amount] / [total amount of iron ore A, B, C, D] [C / g ] [iron ore C amount] / [iron ore a, b, C [Total amount of D] [W,: [Iron ore D amount] / [Iron ore A, B, C, D total measurement]) The average pore volume X of the iron ore defined is 〇〇9cmVg or less In the manner, the sintered ore is produced by the sintering raw material of the iron slag. 2. The method for producing a sintered ore according to claim 1, wherein the sintered raw material is blended with iron ore B. 3. The method for manufacturing a sintered ore according to the first application of the patent scope, wherein, 312XP/invention specification (supplement) pulse 2/9413chuan 9 ^299363 sintering raw material φ # 4 such as τ' with iron ore A, iron Ore beta and iron ore c. Tie Yi Er: The manufacturing method of the sinter of the second item of the second division, wherein the ratio of the 舛θ 戥 ore Α, the iron ore Β, the iron ore C and the iron ore ... is 20% by mass or more. W. D. For example, the method of manufacturing iron ore D for calcium into r Λ in the second paragraph of the patent scope of the application, wherein iron ore A, iron ore Β, iron ore Γ Γ 戚 ^ The ratio of the total amount of n is 2% by mass or more. And iron ore D 312XP/發明說明書(補件)/94-12W134179 32312XP/Invention Manual (supplement)/94-12W134179 32
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