TWI302946B - Self-reducing, cold-bonded pellets - Google Patents
Self-reducing, cold-bonded pellets Download PDFInfo
- Publication number
- TWI302946B TWI302946B TW93127993A TW93127993A TWI302946B TW I302946 B TWI302946 B TW I302946B TW 93127993 A TW93127993 A TW 93127993A TW 93127993 A TW93127993 A TW 93127993A TW I302946 B TWI302946 B TW I302946B
- Authority
- TW
- Taiwan
- Prior art keywords
- pellet
- pellets
- weight
- iron
- cement clinker
- Prior art date
Links
Description
1302946 九、發明說明: 【發明所屬之技術領域】 :發:係有關於一種用於製鐵工業之可自動還原的冷 及其製造的方法。由於該小丸之可自動還 :的=,使得當將該冷結合的小丸加熱至高溫的時候, 丨L 率地使用該小丸來製造鐵和鋼,並且可以將該 部分的《當中’諸如電弧爐(eaf)、轉化 爐:用於製鋼之開放爐床溶爐、鼓風爐、用於製鐵之非鼓 =減以及用於還原直接還原鐵(DRI)i品之直 鐵熔爐。 【先前技術】 )係揭不一種 以及在製鋼業 美國專利案第3,150,958號(Collin等人 還原氧化鐵、和粉末化之含碳材料的方法, 中自動還原小丸之用途的通則。 吳國專利案第3,174,846號(Bdsse等人)係揭示—種 使用遞青煤(bituminous coal )壓塊氧化鐵細粒之方法, 以及揭示其用於鼓風爐進料的用途。 吴國專利案第3,264,G92號(Ban等人)係揭示一種製 造經碳化及金屬化之鐵礦小丸的系統,其係適用於諸如熔 鐵爐(cupola type furnace)或鼓風爐之熔煉操作。 美國專利案第3,323,901號(Dahl等人)係揭示一種 由精細切割之金屬氧化物礦所製成之小丸、_種含碳還原 劑、以及一種亞硫酸鹽稠漿(sulphite lye)或者是糖漿黏 著劑(molasses binder)。 1302946 美國專利案第3,437,474號與美國專利案第3,617,254 號(Imperato )係揭示_種從金屬礦/驗土族金屬氧化物、 以及氫氧化物/含碳材料(例如煤)製造大塊礦石。u— ore )的方法,5亥煤塊在有濕氣存在之下與二氧化碳互相反 應’其係適用於製鋼的熔爐。 吳國專利案第3,49M95號(Svenss()n等人)係揭示 種用於~硬化小丸的方法’該小丸含有鐵礦精砂、精細 切告J之波特蘭水泥熟料和水。將生的小丸鑲嵌至大量離散 ,精細切割的鐵礦微粒中。當小丸具有可接受之強度時, 違镶肷之團塊就會被小丸給分離。 、美國專利案第35938,987號(Ban)係揭示一種由氧化 鐵所开y成之小丸’其具有非黏聚性的缺點,而其巾將這此 小丸於-活動閘門機器中進行燒結,加入了從外部供應: 3奴材料於5亥燒結床中,足以彌補該小丸中的缺點。 美國專利案第45〇49,435號(L〇t〇sh等人)係揭示使 用種廣物水性黏著劑來混合一礦物,同時將該所獲得之 此口物進仃均質化、並活化,然後再將該混合物進行小 化(pelleUzed ) ’並將生的煤塊進行熱濕處理(kat h_ treatment)、夺σ 今议 ^ ^ 和之後的二階段加熱處理。 美國專利案第4,G93,448號(Eliseev等人) 用一種具有渥度U 15%以及微粒尺寸小於G83、f^ 礦石細粒、以及—種氧㈣和氧化鎂形式之黏結材 備-種混合物。然後將該混合物進行水合處理,並首^ 礦石細粒中以製造出一種具有4至15重量百分比 之霉占為 1302946 材料的均質混合缺 中孰介+ …、傻將°亥均質混合物藉由在飽和蒸氣 中纽’來進行小丸化,以製成小丸。 ^國:利案第4,168,966號(Furui等人)係揭示-種 係用於包含似水泥之材料的鼓風爐,並加以調 :=—1〇2的比例於12至19的範圍之中,以 離ίΓ比率在13119%㈣圍之中。將該經形成之 黏聚物在不沒有粉末基材的情形下,於導入至 "亥k爐之前進行熟化。 :國專利案第4,52M29號(GQksel等人)係揭示一 _備經滋潤之礦石細粒混合物,所製造之含氧化鐵 =的自動遷原黏聚物;一種精細切割之天然熱解的含碳 σ、料’大@ 1至大約30重量%的黏結劑,諸如經燒石灰 火,以及一種介將其於壓力下與蒸氣相接觸以將該 生的黏5^物進行水熱硬化。 …美國專利案第4,636,342號(Miyashlta等人)係揭示 連續供應一種含有經碳酸化之黏結劑的生小丸至一垂直型 、之反杰中,以進行連續將該生小丸依序通過一預乾燥 區、一碳酸化區、以及在該垂直型式反應器中的乾燥區; 將預乾焯氣體吹入至該預乾燥區中,以將其中之該生小 丸進行預乾燥;將一包括5至95體積%二氧化碳與5至95 體積%飽和蒸氣之碳酸化氣體吹入該碳酸化區域中,以將 忒包含在生小丸中之碳酸化黏結劑進行碳酸化;以及將一 乾刼氣體吹入至該乾燥區域中以將其中之生小丸進行硬 化。 1302946 一美國專利案第4,84M84號(Shigematsu等人)係揭 2將波特蘭水泥、鼓風爐水泥或者是鼓風爐熔渣進行混 口其iT、藉由與具有鐵礦細粒之黏結劑來加以混合,以形 :大的塊狀物。然後將該塊狀物進行熟化或硬化、並加以 ?卞此方法的缺點在於高溫壓縮強度會被降低至比要求 遂低而且要獲得小丸所須之自動還原品質是很困難的。 μ美國專利案第5,G6M27號(Yanaka #人)使用了水 泥來做為一黏結劑,並且藉由添加水來將該具有鐵礦細粒 之水泥及/或含碳物質進行混合,以形成生的小丸。在將 該生白M、丸放置到-移動式爐柵上之後,再將該小丸以一 具有一虱化碳濃度為55體積%或更多的氣體進行處理。 此=法的缺點在於該所需之二氧化碳太高,反而要獲得工 業環境中較高品質變的很困難。 吴國專利案第6,334,883號(Takenaka等人)係揭示 了包含含碳材料之小丸以及主要由氧化鐵所構成之鐵礦。 在摩人化及合化過私中,該含碳材料之最大流動率以及在該 鐵礦中lOmu.m或更小之氧化鐵微粒的比率係落於一特定 的範圍中。 美國專利案第6,4〇9,964號(Aota等人)係揭示包含 微粒鐵材料之形狀主體’諸如鑄造小丸、壓塊、及其相似 者,並具有足夠的強度來抵抗高達至少1〇〇(rc之溫度,其 可藉由使用凡王水合化之㊉氧化I呂水泥來做為黏結劑。在 這些小丸當中係使用大尺寸微粒的鐵礦,因此,該小丸之 逛原速度相對的較慢。由於所使用的材料以及製造方法, 1302946 使侍藉由此方法所製造出來的小丸對於自動還原的領域有 困難。並且,在某些熔融製程當中會不希冀高氧化鋁含量 勺^結劑’因為其會增加溶渣的氧化铭含量。 美國專利案第6,565,623號(Contmcci等人)係揭示 在大約70至大約10(rc的溫度和大氣壓力下,於飽和蒸氣 存在的情形,將包含水泥做為黏結劑之自動還原的黏聚物 進仃熟化和乾燥。該自動還原之黏聚物是由下列成分之混 口物所構成:鐵礦細粒及/或包含氧化鐵之工業殘渣及/ 或金屬鐵、含碳材料的細粒,諸如礦煤、木炭、生石油焦 (green petroleum coke)以及相似的細粒;助熔材料,諸 如煉鋼薇熔渣和鼓風爐熔渣、石灰石、石灰、以及相似的 材料;做為黏結劑之水泥;助熔劑;以及介於7和12%的 座度。此方法係使用蒸氣將該水泥塊熟化,但是因為該生 的水泥塊具有低的壓縮強度,因此該生的水泥塊就必須將 其預先乾爍’以降低水的含量,並試圖藉此增加該生水泥 塊的壓縮強度。然而,該預先乾燥生水泥塊的方法將會讓 5亥生的水泥塊無法充分地進行水合,並且降低最終產物之 壓縮強度的品質。其冷壓縮強度被認為低於所希冀的平均 值,並且只有在範圍大約17-50 kgf/小丸之間。 目前正在針對鐵和鋼材之熔融技術所進行的研發,諸 如直接鋼製造技術、熔融還原鐵製造(smelt-reduction iron-making )技術、DRI技術、將鼓風爐中之焦炭與金屬 之比例降低的技術、以及使用冷結合之小丸做為鼓風爐進 料來取代燒結物的鐵製造技術,其中所面臨最大的問題就 1302946 是如何在工鞏制、Α 對低的成本所有㈣Μ融條件下,以相 有鑑於此,研 、高效率、且快速還原之鐵礦。 研發具有自動還原能力之冷 解決此問題的—個重要的方法。 ^口黏編成為 有-個習知的方法稱為规方法,該謂法 了 一個預先還原的階段 ' ATST古、ϋ 仅乂及個熔嘁遏原的階段。在該 鐵垆」:’係將經過預先加熱、和部份進行預先還原的1302946 IX. Description of the invention: [Technical field to which the invention pertains]: Hair: A method for cold reduction and its manufacture for use in the iron industry. Since the pellet can be automatically returned to the temperature, the pellet is used to produce iron and steel when the cold-bonded pellet is heated to a high temperature, and the portion of the "middle" such as an electric arc furnace can be used. (eaf), reformer: open hearth furnace for steel making, blast furnace, non-drum = reduction for iron making, and straight iron furnace for reducing direct reduced iron (DRI). [Prior Art] is a general rule for the use of automatic reduction pellets in the method of reducing iron oxide and powdered carbonaceous materials in the steelmaking industry, U.S. Patent No. 3,150,958. Patent No. 3,174,846 (Bdsse et al.) discloses a method for using a bituminous coal compacted iron oxide fine particle and discloses its use for blast furnace feed. Wu Guo Patent No. 3,264 , G92 (Ban et al.) discloses a system for producing carbonized and metallized iron ore pellets suitable for use in a smelting operation such as a cupola type furnace or a blast furnace. U.S. Patent No. 3,323,901 ( Dahl et al.) discloses a pellet made of finely cut metal oxide ore, a carbonaceous reducing agent, and a sulphite lye or a molasses binder. U.S. Patent No. 3, 437, 474 and U.S. Patent No. 3, 617, 254 (Imperato) disclose metal oxide/soil test metal oxides and hydroxide/carbonaceous materials ( The coal) producing lump ores .u- ore) method, 5 Hai coal in the presence of moisture and carbon dioxide under reaction with each other 'system which is suitable for steel making furnace. Wu Guo Patent No. 3, 49M95 (Svenss () n et al.) discloses a method for ~ hardening pellets. The pellet contains iron ore fine sand, fine Portland cement clinker and water. The raw pellets are inlaid into a large number of discrete, finely cut iron ore particles. When the pellets have an acceptable strength, the agglomerates will be separated by pellets. U.S. Patent No. 35,938,987 (Ban) discloses a pellet which is made of iron oxide, which has the disadvantage of being non-cohesive, and the towel sinters the pellet in a movable gate machine. Added from the outside supply: 3 slave material in the 5 Hai sintering bed, enough to make up for the shortcomings in the pellet. U.S. Patent No. 4,490,435 (L〇t〇sh et al.) discloses the use of a wide-area aqueous adhesive to mix a mineral while homogenizing and activating the obtained mouth. The mixture is then subjected to miniaturization (pelleUzed) and the raw coal mass is subjected to a heat-moisture treatment (kat h_treatment), a sigma- tion, and a subsequent two-stage heat treatment. U.S. Patent No. 4, G93,448 (Eliseev et al.) uses a binder having a twist U 15% and a particle size smaller than G83, f^ ore fines, and oxygen (tetra) and magnesium oxide. mixture. The mixture is then subjected to hydration treatment, and the first ore fines are used to produce a homogeneous mixture of 4 to 15 weight percent of the mildew of the material 1302946, and the silly homogenous mixture is The saturated vapor is used to make pellets to make pellets. ^Country: No. 4,168,966 (Furui et al.) reveals that the germline is used in a blast furnace containing cement-like materials and is adjusted: the ratio of =-1〇2 is in the range of 12 to 19, The ratio is between 13119% (four). The formed cohesive polymer was aged before being introduced into the "Heil furnace without the powder substrate. : National Patent No. 4, 52M29 (GQksel et al.) reveals a mixture of finely granulated ore fines, which is made of iron oxide-containing automatic migration of the original; a finely cut natural pyrolysis A binder containing carbon σ, material 'large @ 1 to about 30% by weight, such as a burnt lime fire, and a medium which is contacted with a vapor under pressure to hydrothermally cure the raw adhesive. U.S. Patent No. 4,636,342 (Miyashlta et al.) discloses the continuous supply of a raw pellet containing a carbonated binder to a vertical type, which is used to continuously pass the raw pellet through a pre-drying process. a zone, a carbonation zone, and a drying zone in the vertical type reactor; pre-drying gas is blown into the pre-drying zone to pre-dry the pellet therein; one comprising 5 to 95 a carbonation gas of 5% by volume of carbon dioxide and 5 to 95% by volume of saturated steam is blown into the carbonation zone to carbonate the carbonation binder contained in the granules; and a dry krypton gas is blown into the drying In the area, the pellets are hardened. 1302946 A U.S. Patent No. 4,84M84 (Shigematsu et al.) discloses that Portland cement, blast furnace cement or blast furnace slag is mixed with its iT, by means of a binder with iron ore fines. Mix to shape: large chunks. The block is then aged or hardened, and the disadvantage of this method is that the high temperature compressive strength is lowered to a lower level than required and it is difficult to obtain the automatic reduction quality required for the pellet. μ US Patent No. 5, G6M27 (Yanaka #人) uses cement as a binder, and by adding water to mix the cement and/or carbonaceous material with fine iron ore to form Raw pellets. After the greening M and pellets were placed on the mobile grate, the pellet was treated with a gas having a deuterated carbon concentration of 55 vol% or more. The disadvantage of this method is that the carbon dioxide required is too high, and it is difficult to obtain higher quality in the industrial environment. U.S. Patent No. 6,334,883 (Takenaka et al.) discloses a pellet comprising a carbonaceous material and an iron ore mainly composed of iron oxide. In the humanization and integration, the maximum flow rate of the carbonaceous material and the ratio of iron oxide particles of 10 mol% or less in the iron ore are within a specific range. U.S. Patent No. 6,4,9,964 (Aota et al.) discloses the shape of a body comprising a particulate iron material such as cast pellets, briquettes, and the like, and having sufficient strength to resist up to at least 1 〇〇 ( The temperature of rc can be used as a binder by using the oxidized Ilu cement of Van Gogh. In these pellets, iron ore of large size particles is used, so the original speed of the pellet is relatively slow. Due to the materials used and the manufacturing method, 1302946 makes it difficult for the pellets produced by this method to be in the field of automatic reduction. Moreover, in some melting processes, it is not desirable to have a high alumina content scooping agent. Because it increases the oxidized content of the slag. U.S. Patent No. 6,565,623 (Contmcci et al.) discloses that in the presence of saturated steam at temperatures of about 70 to about 10 (rc and atmospheric pressure, cement will be included). The self-reducing cohesive agent for the binder is aged and dried. The auto-reduced mucopolymer is composed of a mixture of iron ore fines and/or iron oxide. Industrial residues and / or metal iron, fine particles of carbonaceous materials, such as coal, charcoal, green petroleum coke and similar fine particles; fluxing materials, such as steel slag and blast furnace slag , limestone, lime, and similar materials; cement as a binder; flux; and a seat between 7 and 12%. This method uses steam to mature the cement block, but because the cement block has Low compressive strength, so the green cement block must be pre-dryed to reduce the water content, and try to increase the compressive strength of the green cement block. However, the method of pre-drying the green cement block will The 5th cement block is not sufficiently hydrated and the quality of the final product is reduced. The cold compressive strength is considered to be lower than the expected average and is only in the range of about 17-50 kgf/pill. Research and development on iron and steel melting technologies, such as direct steel manufacturing technology, smelt-reduction iron-making technology, DRI technology, The technology of reducing the ratio of coke to metal in the blast furnace, and the iron manufacturing technology using the cold combined pellet as the blast furnace feed to replace the sinter, the biggest problem facing 1302946 is how to work, Low cost All (4) Under the conditions of smelting, in view of this, research, high efficiency, and rapid reduction of iron ore. Research and development of an automatic method with automatic reduction ability to solve this problem - an important method - A conventional method called the gauge method, which is a pre-reduction stage 'ATST ancient, ϋ only 乂 and a melting stagnation stage. In the shovel: 'The system will be preheated, and Partially pre-reduced
:Γ煤、或焦炭炭渣(c〇ke —、以及助溶劑 攸頂4進枓至一個經加壓的熔融反應器中,該反應器包括 了:熔融浴的鐵和熔渣。該煤在熔融潰層當中進行液化,: strontium coal, or coke carbon slag (c〇ke -, and cosolvent dome 4) is fed to a pressurized melt reactor comprising: iron and slag of the molten bath. Liquefaction in the melted layer,
而:鐵礦:】、丸熔化至該熔渣之中,之後藉由熔渣中的碳 (炭)而還原。該方法條件使得熔渣起泡。在該方法中所 產生之一氧化碳與氫氣在該熔渣層之中或者是其上方進行 後燃燒處理,以提供該吸熱還原反應所需的能量。將氧氣 從頂部吹入,通過一個中央水冷卻的吹管,並將氮氣注入 通過在該反應器下方之風口,以確保有充分的攪拌,促進 該後燃燒能量能夠進行熱傳輸至該浴之中。將該方法之廢 氣於一熱旋風中進行除塵,之後再將其飼入至一高爐中以 對該小丸進行預加熱並且預先還原成Fe〇或方鐵礦 (wustitle ) 〇 還有一個習知的方法稱為COREX.RTM方法Q Corexrtm 是 Deutsche Voest_Alpine Industrieanlagenbau GMBH andAnd: iron ore:], the pellet is melted into the slag, and then reduced by carbon (char) in the slag. The process conditions cause the slag to foam. One of the carbon monoxide and hydrogen produced in the process is post-combusted in or over the slag layer to provide the energy required for the endothermic reduction reaction. Oxygen is blown from the top through a central water-cooled blow tube and nitrogen is injected through the tuyere below the reactor to ensure adequate agitation to promote heat transfer to the bath. The exhaust gas of the method is dedusted in a hot cyclone, and then fed into a blast furnace to preheat the pellet and pre-reduced into Fe or wrought iron (wustitle). There is also a conventional The method called COREX.RTM method Q Corexrtm is Deutsche Voest_Alpine Industrieanlagenbau GMBH and
Voest A!pi7te IndustHeanlagenbau 的一個商標名)。在兮 方法中,是在兩個製程反應器當中進行冶金加 11 1302946 工’此兩個製程反應器為:還原熔爐與熔融氣化器。使用 非煉焦煤(non-coking c0ais)以及具有諸如大塊礦石 '小 丸、或燒結物的鐵,製造出具有鼓風爐品質的熱金屬。將 煤通過一氣壓閥(Pressure lock )系統,進入至該炼融氣 化裔的圓頂,在該熔融氣化器中於1,丨〇〇至1,丨5〇〇c的溫度 範圍中會發生煤的破壞性蒸餾。吹入至該熔融氣化器之中 的氧氣會從該經導入的煤而製造出焦炭床,並且導致具有 95% CO+札以及大約2%的c〇2所構成的還原氣體。該Voest A!pi7te A trade name for IndustHeanlagenbau). In the 兮 method, metallurgical addition is carried out in two process reactors. The two process reactors are: a reduction furnace and a melter gasifier. The use of non-coking c0ais and iron with large ore 'pellets, or sinter, produces hot metal with blast furnace quality. Passing the coal through a Pressure Lock system into the dome of the liquefied gasification, in the temperature range of 1, 丨〇〇 to 1, 丨5〇〇c in the melter gasifier Destructive distillation of coal occurs. Oxygen blown into the melter gasifier produces a coke bed from the introduced coal and results in a reducing gas composed of 95% CO + sag and about 2% c 〇 2 . The
氣體會排出該熔融氣化器之外,然後被除塵、並且被冷卻 至介於800°C和850°C之所希冀的還原溫度範圍。然後將 该氣體用來將還原熔爐中的大塊礦石、小丸或燒結物,還 原成具有平均金屬化程度高於90%的海綿鐵。使用一種特 殊叹计的螺旋輸送機將該海綿鐵取出,並滴落至該熔融氣 化态之中,熔化成熱的金屬。如同在鼓風爐之中一般,石 灰石凋整了溶渣的驗度,以確保硫有從該熱金屬移除。取 决於所使用的鐵礦,同樣可以將Si〇2進料至該系統之中,The gas exits the melter and is then dedusted and cooled to a range of reduction temperatures between 800 °C and 850 °C. The gas is then used to reduce the bulk ore, pellets or sinter in the reduction furnace to sponge iron having an average degree of metallization of greater than 90%. The sponge iron is taken out using a special auger screw conveyor and dropped into the molten gas state to be melted into a hot metal. As in the blast furnace, the limestone has withdrawn the slag to ensure that the sulfur is removed from the hot metal. Depending on the iron ore used, Si〇2 can also be fed into the system.
以調整其化學組成以及熔渣的黏度。出鋼程序與溫度、以 及熱金屬組成均完全與鼓風爐之中相同。該還原炫爐之頂 部氣體具有大約7,_ KJ/Nm3的總發熱值,並且可以被 用在各種廣泛的應用中。 冷結合方法係定義為一 一種具有預先決定之尺寸以 聚物。此係藉由將包含氧化 加劑加以混合的方式而完成 種物理和化學方法,以製造出 及足夠強度和使用耐久性的黏 鐵的材料、黏結劑、及/或添 以藉由使用小丸化的機器來 12 1302946 生成生的小丸。在該小丸均被小丸化之後,通常是經該生 的小丸進行熟化。 該冷結合方法通常是由在小丸之中所使用之黏結劑的 種類、以及熟化該小丸的方法來加以分類。舉例而言,水 硬性結合(hydraulic bond)、碳酸鹽結合、熱—水硬性結 合(therm〇_hydraulic b〇nd )、索雷水泥結合(cement )、 液態玻璃結合、以及其他有機結合劑結合,都是在過去都 已經經過分析與運用的方法,但是都得到了無法令人滿意 的結果。卩下有兩個實施例說明水硬性和碳酸鹽冷結合“ 該水硬性結合方法係使用水硬性物質來做為黏結劑。 :4而。在此方法中所使用的水泥係由波特蘭水泥、高 氧化铭水泥、鼓風爐水泥、或者是鼓風爐溶潰所構成。也 有使用的有石灰、消石灰(hydr〇_llme)、以及其他。在 將該黏結劑與包含氧化鐵之材料混合並添加水之後,㈣ 成了小丸。之後,在將該小丸進行乾燥和硬化。典型射 硬性結合方法係使用波特蘭水泥來做為黏結劑。 該碳酸鹽結合方法係使用石灰、消石灰、或者是 包含石灰的材料來做為黏結劑。 八 人+ 在將该黏結劑與鐵礦細粒 冼合在一起,而形成小丸之後, 碳之熱氣體進行熟化。包含在 ^'肖“含二氧化 匕3在邊小丸之中的氫氧化鈣盥二 氧化碳進行反應,以生成碳酸鈣, 隨即獲得適當㈣度與耐A性。 在此以,該小丸 所有的冷結合方法到目前兔 為止都已經證實在實際應用 13 1302946 當中是無效果的。其原因在於所有的方法均具有至少一個 缺點導致以下的缺陷:低的冷壓縮強度、無法令人滿音的 u原降解指數、低的高溫強度、不適當的可還原性:高製 &成本、或者是無法製造連續大量的卫業用鐵或鋼材。 么由於其他習知的冷結合黏結劑無法確實達到廣泛冶金 能的需求,或者是在低成本之條件下完成連續的工業製 ^使得這些現有的技術仍然無法歧地運用至鐵和鋼工' 業:中。MTU含碳小丸可以部分地放置於_個用於製造鐵 的政風爐當令,以及一個用於製鋼的電爐、和用於製鐵的 =爐當中,但是該小丸無法在低成本的條件下被放置到 的了且大規格的生產線上’因此就工業界而言是無法運用 因此’本發明的目的在於利 小丸的方法,來解決以上所提和一種用於製備該 際操作當中。 丨料及的問題’以將其運用製實 【發明内容】 本發明的目的在於提供—種自動還原、冷結合之小丸 :及一種製造該小丸之方法,以用於炼融多種鋼材,包括 妓風爐製鐵、非鼓風爐製鐵、以及在 類的製鋼,等等m…士人 i甲之所有種 或廢氣、或者是任何:=5之小丸的期間,沒有水、 原料是报廣泛的,而I可非放。在這些小丸當中之 出來的亞鐵灰塵、或事鋼,^王使用由鐵和鋼材廢所製造 小丸的製造成本係低於習知之 广 '、观f性的產品,且其投資 14 1302946 資本係少於燒結物的一 f ,、、 1 +。因此,本發明可以大幅度降低 製造成本以及鐵和鋼材廠之不可避免的污染。 ▲ /自動延原、冷結合之小丸包括了鐵礦精砂、含碳還 原片丨X及具有特殊需求做為黏結劑之精細切割的波特蘭 水泥熟料。將這此赤八έ士人+ ^ 一成刀、、、口 5在一起以形成一混合物。當該 混合物被放置在一 j古办世# ,, , 牡衣狀碟盤中、或者是一旋轉筒中,並加 入水’則產生了小丸。藉由使用滾筒篩(roller screens ) 而獲得具有預先決定之尺寸的小丸,正常是在8·ΐ6疆之 間。然後再將該小丸連續放置到一熟化裝置之中。在該孰 · 化裝置内部’藉由使用具有大約1〇〇·3〇〇χ:之溫度且包含 二氧化碳的熱氣體’來將該小丸將進行水合、以及碳酸化 (carbonated)。之後’於乾燥之後,將該經乾燥之小丸 從該熟化裝置中排放出來,就可以準備使用。 本發明提供了以下優於先前技術的優點: (1 )可以使用所有種類之現有的製鋼熔爐、以及相 關的技術機制,無須再重新以高投資成本進行重建組織; (2 )本發明所使用之新的小丸,其製造成本遠低於 _ 那些預先還原之小丸以及經燒成之小丸的成本;可以進行 連續的工業製造,而且不會製造污染; (3 )由於可以使用所有種類之精砂細粒以及低成本 的赤鐵礦細粒(hematite fines),並且亦可以部分添加來 自於鋼材工業之含鐵灰塵,諸如Unz_D〇nawitz (LD)製 鋼於泥,對於不同的鐵礦而言都可以達到高的可挽性· (4 )較低的能量消耗;以及 15 1302946 此 (5 )可以將該新的小丸用於a 可降低該製鋼成本高達2⑽。 _ EAFfe爐中 該自動還原、冷妙人 原劑、以及具有特破雨击、匕了鐵礦精砂、含碳還 水泥孰料。兮料# # , w之精細切割的波特蘭 鋼於泥、:奋备丨棘丄匕 斤構成’遠如製 主要的部分岸兮4。該鐵礦精砂之最 為… 約200目(mesh)或者是更小,較佳 為介於大約200目和325目 竿乂1 度。9 # # # I θ 則其會降低小丸的強 争鐵礦精砂之鐵含量正常情形應該為大約_或者是 更同,其亦可為與鐵礦細粒互相 ^ 丨山士 仲此σ之此合物。該包含在 小丸中之鐵礦精砂的數量係 .^ ^ 里竹取决於其鐵的含量以及還原劑 L數量,且正常情形下係介於大約6 之間。 里里/〇 該含碳還原劑典型地係為煤粉末。其可由焦炭炭清、 無煙煤、或者是其混合物所構成。包含在這些含碳材料之 中的固定碳數量’正常情形下為大約70%或者是更高,越 高越好。該煤粉末應該要具有超過大肖95%的微粒,該微 粒具有小於大,約Q3 _之尺寸,換句話說,該煤粉末微 粒必須要為大約48目或者是更少,就製鐵而言正常情形 下大約為60目,就製鋼而言大約為2〇〇目。包含在該小 丸之中的煤含量係取決於包含在該小丸中之氧化鐵(。— 11 on )數1以及該煤之固定碳含量,且其應該要為至少一 個數值,該數值能夠使得90重量%的鐵含量從包含在該 16 !3〇2946 小丸中之總氧化鐵還原回來;否則,其將會降低了該小丸 =熱強度。在計算包含在該小丸之中的煤數值時,該熱平 衡同樣應該要被考慮進去。在正常情形下,該煤含量的範 圍是在大約10-26重量%之間。 4 一、、Ό背]係為具有特殊需求之精細研磨的波特蘭水泥 沾料’使付其會讓該小丸具有高的早期強度、良好的水合 作用和石反酸化的品質,也使得該小丸在反應裝置中熟化以 後’會具有高強度及自動還原的特性。習知的是,包含在 水泥热料中之石夕酸二鈣(dicalcium siHcate)相較於包含在 _ 波特蘭水泥熟料中之矽酸三鈣、鋁酸三鈣(⑴⑶…咖 aluminate )、鹤鐵石(brown millerite )而言具有最慢的 火a作用速度。该石夕酸二飼會大大地影響該小丸的強度, 使得其含量必須要降低至一種程度,即少於2〇重量%, 較佳為少於8重量%。該水泥熟料之其他需求如下: (1 )包含在水泥熟料中之矽酸三舞應該要具有超過 大約50重量%的含量,最理想的含量為大約56重量%,To adjust its chemical composition and the viscosity of the slag. The tapping procedure and temperature, as well as the composition of the hot metal, are identical to those in the blast furnace. The top gas of the reduction furnace has a total calorific value of about 7, _ KJ / Nm3 and can be used in a wide variety of applications. The cold bonding process is defined as a polymer having a predetermined size. This is accomplished by a combination of oxidative additions to accomplish physical and chemical methods to produce a material of sufficient strength and durability to use iron, binders, and/or fillers by using pelletization. The machine came to 12 1302946 to generate raw pellets. After the pellets are all pelletized, they are usually matured by the pellets of the raw. The cold bonding method is usually classified by the kind of the binder used in the pellets and the method of ripening the pellets. For example, hydraulic bonds, carbonate bonds, thermo-hydraulic b〇nds, soare cements, liquid glass bonds, and other organic binders, They have all been analyzed and applied in the past, but they all have unsatisfactory results. There are two examples in the underarm that illustrate the combination of hydraulic and carbonate cold. "The hydraulic combination method uses a hydraulic material as a binder. :4. The cement used in this method is Portland cement. , high-oxidation cement, blast furnace cement, or blast furnace melting. Also used are lime, hydrated lime (hydr〇_llme), and others. After mixing the binder with the material containing iron oxide and adding water (4) becomes a pellet. After that, the pellet is dried and hardened. The typical shot-bonding method uses Portland cement as a binder. The carbonate combination method uses lime, slaked lime, or contains lime. The material is used as a binder. Eight people + After the binder is combined with the fine particles of iron ore, and the pellets are formed, the hot gas of carbon is matured. It is contained in the side of the 'Xiao' containing cerium oxide 3 Calcium hydroxide and carbon dioxide in the pellets are reacted to form calcium carbonate, and then appropriate (four) degrees and resistance to A are obtained. Here, all the cold-binding methods of the pellets have been confirmed to be ineffective in practical application 13 1302946 until now. The reason for this is that all methods have at least one disadvantage that leads to the following drawbacks: low cold compressive strength, unproducible u-origin degradation index, low high-temperature strength, and inappropriate reducibility: high system & cost Or it is impossible to manufacture a large number of continuous use of iron or steel for the industry. Because other conventional cold bond adhesives can't really meet the needs of a wide range of metallurgical energies, or to complete continuous industrial processes at low cost, these existing technologies are still inextricably applied to iron and steel industry. :in. The MTU carbonaceous pellets can be partially placed in a steel furnace for the manufacture of iron, as well as an electric furnace for steel making and a furnace for iron making, but the pellet cannot be used at low cost. The large-sized production line that has been placed on the production line is therefore incapable of being used in the industry. Therefore, the present invention aims to solve the above-mentioned operations and to prepare for the preparation of the process.丨 及 ' 以 以 以 以 以 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 【 Furnace iron, non-blast furnace iron, and steel in the class, etc., during the period of all kinds of materials or waste gas, or any pellets of =5, no water, raw materials are widely reported, and I can not put it. In the ferrous powder dust or steel that comes out of these pellets, the manufacturing cost of the pellets made from iron and steel waste is lower than that of the well-known products, and its investment is 14 1302946. Less than a f, ,, 1 + of the sinter. Therefore, the present invention can greatly reduce the manufacturing cost and the inevitable pollution of the iron and steel plants. ▲ / Automatic extension and cold combination pellets include iron ore concentrate, carbon-reducing film X and fine-cut Portland cement clinker with special requirements as a binder. Put this red bastard + ^ into a knife, and mouth 5 together to form a mixture. The pellet is produced when the mixture is placed in a j-shop, a crepe dish, or a rotating drum, and water is added. Pellets having a predetermined size are obtained by using roller screens, which are normally between 8·ΐ6. The pellets are then placed continuously into a curing apparatus. The pellets are hydrated and carbonated by using a hot gas having a temperature of about 1 Torr and containing carbon dioxide inside the hydrazine device. After drying, the dried pellets are discharged from the curing apparatus and ready for use. The present invention provides the following advantages over the prior art: (1) It is possible to use all kinds of existing steelmaking furnaces, and related technical mechanisms, without having to rebuild the tissue at a high investment cost; (2) used in the present invention The new pellets are much cheaper to manufacture than the cost of pre-reduced pellets and calcined pellets; they can be manufactured in continuous industrial production without contamination; (3) because all types of fine sand can be used Granules and low-cost hematite fines, and may also partially contain iron-containing dust from the steel industry, such as Unz_D〇nawitz (LD) steel in mud, which can be achieved for different iron ore High manageability · (4) Lower energy consumption; and 15 1302946 This (5) can be used for a new pellet to reduce the steelmaking cost by up to 2 (10). _ EAFfe furnace This automatic reduction, cold and artificial agent, as well as with special broken rain, iron ore fine sand, carbon and cement.兮料# # , w finely cut Portland steel in the mud,: 奋 丨 丨 斤 斤 斤 斤 斤 ’ ’ ’ ’ ’ ’ ’ ’ ’ ’ 主要 主要 主要 主要 主要 主要 主要 主要 主要 主要The iron ore fine sand is most preferably about 200 mesh or less, preferably about 200 mesh and 325 mesh 竿乂 1 degree. 9 # # # I θ, it will reduce the strength of the pellets. The iron content of the iron ore concentrate should be about _ or more. It can also be combined with iron ore fines. This compound. The amount of iron ore concentrate contained in the pellets is determined by the amount of iron and the amount of reducing agent L, and is normally between about 6.里里/〇 The carbonaceous reducing agent is typically a coal powder. It may consist of coke bromide, anthracite, or a mixture thereof. The amount of fixed carbon contained in these carbonaceous materials is normally about 70% or higher, and the higher the better. The coal powder should have more than 95% of the particles of the large xiao, the particles having a size smaller than about, about Q3 _, in other words, the coal powder particles must be about 48 mesh or less, in terms of iron production. It is about 60 mesh under normal conditions and about 2 mesh in steel. The coal content contained in the pellets depends on the iron oxide (?-11 on) number 1 contained in the pellet and the fixed carbon content of the coal, and it should be at least one value which enables 90 The iron content by weight % is reduced back from the total iron oxide contained in the 16!3〇2946 pellet; otherwise, it will reduce the pellet=thermal strength. When calculating the value of coal contained in the pellet, the thermal balance should also be taken into account. Under normal conditions, the coal content ranges between about 10 and 26% by weight. 4 I., Hatchback] is a finely ground Portland cement dip with special needs. It will make the pellet have high early strength, good hydration and stone acidification quality. The pellets will have high strength and auto-reduction characteristics after being matured in the reaction apparatus. It is known that dicalcium siHcate contained in cement hot material is compared with tricalcium citrate and tricalcium aluminate contained in _ Portland cement clinker ((1)(3)...aluminate) In the case of brown millerite, it has the slowest fire a speed. The diteric acid feed will greatly affect the strength of the pellet so that its content must be reduced to a degree that is less than 2% by weight, preferably less than 8% by weight. Other requirements for the cement clinker are as follows: (1) The tannins included in the cement clinker should have a content of more than about 50% by weight, most preferably about 56% by weight.
越南越好; 4P (2 )石夕酸三鈣和鋁酸三鈣之體積應該要有介於大約 5 · 1至1 〇 · 1的範圍之間的比例; (3 )該水泥熟料應該要被精細切割,使得量測出來 小於0·08 mm之微粒尺寸的部分應該有大約90%或者是更 大的體積; (4 )游離氧化飼(free calcium oxide,f-CaO )含量 應該要少於3重量%。 17 1302946 如果該黏結劑係少於大約1〇% ,則該小丸將具有低的 壓細強度’但是如果該黏結劑係超過大約20% ,也將會使 付忒小丸使用起來相對較為昂貴。在正常情形下,該小丸 之黏結劑含置是落於大約1〇_2〇重量%的範圍之間。 在某些例子當中,可添加範圍在大約0-3重量%的添 加劑於戎小丸當中。該添加劑可由以下所構成:白雲石 (dolomite)、石灰石、石灰、消石灰、息土( ^處、 亂化妈、以及任何一種其他可調整驗度、炼渣特徵、和小 丸強度的材料。該微粒尺寸應該為大約48目或者是更小。馨 该小丸之成分係為大約6〇_79重量%的鐵礦精砂、大 、勺10 26重里/G的含碳還原劑、以及大約重量%之 具有特殊需求之精細研磨的波特蘭水泥熟料,總合重量為 100% 〇 根據以上所提及預先決定之材料的重量比例所混合, 而創造出—種為了製造小丸的等向性混合物。胃混合物被 «到-小丸化裝置當中,諸如—球狀碟冑、或者是一旋 轉筒中’以藉由添加足夠之水來形成小丸。之後,再將該 小丸於线中進行自然熟化,或者是藉由工業熟化製程將 其進行熟化,如以下所敘述。 在小丸化之I,將該小丸進行分類,諸如利用滾筒筛 末加以過滤’這是因為要將所不希冀之較小或較大的小丸 加以分離’並且排除黏附於該小丸上之鬆散粉末、或 使其更牢固的黏附於該小丸上。排除或者是鞏固小 政知末的目的疋為了要避免當其通過該反應裝置的時候, 18 l3〇2946 J丸之間因為鬆散粉末而黏附在一。 崙扒士 之後’該額外的數 q末和較小或較大的小丸可以再進行回收並再次將a 化。包含於生的小丸中的水正常情形、^、、 舌旦〇/ , Μ 文备在大約8 -12 重里%的範圍之間。 " = 然後將小丸從該反應裝置1〇之頂部入口 作用2 ❹反應裝置1 Q之中,以進行小丸的水合 乍用、石反酸化作用、以及乾燥化。 種單獨垂直的柙,直且有A n。 置1 0係為- ”曰其具有-入口 12於其頂部,一出 =底部’並且在該槽之中以系統的方式分割成上半部 6人下半部1 8 ’該熟化氣體被導人至該反應裝置工◦ 之下+部1 8之中,並且在分別與該槽之上半部工6和下 ΠΓΓ丸相接觸以後,從該槽的入口 12排放出 來胃然,该反應裝置10可以具有多重的入口和出口, 如果有需要的話。該熟化氣體大部分係為—料大於⑽_ =下,包含大約10體積"者是更高之二氧化碳的 廢氣,並且是從工業用爐而來,諸如熱的鼓風爐窒。 "將該小丸依序並連續地分別通過該反應裳置工〇之上 +部1 6與下半部1 8。當向下前進至該上半部1 6的時 候,料丸被緩慢地加熱、並且藉由來自於下半部! 8之 ^二氧化碳的熟化氣體以及來自於下方之小丸所蒸發的 療氣進行熟化。當該小丸前進至該反應裝置工〇之下半部 1 8的内部時,該小丸將被加熱,並且藉由具有大約__ 3〇〇°C溫度範圍之包含二氧化碳的熟化氣體、以及來自於 下方之小丸所蒸發的蒸氣進行熟化。在從反應裝置工〇之 19 1302946 入口 1 2至出口 i 4的路線中,該小丸將依序並連續地藉 由主要水合作、水合作用和碳酸化作用、主要為碳酸化 作用、以及乾燥(desiccati〇n)來進行熟化。並且,該小 丸經會充分地進行水合、碳酸化、以及乾燥。 一旦從該反應裝置1 〇中排放出來,該小丸即準備好 可以進行利用。從小丸自反應裝置i 〇之入口丄2進入開 =到結束’並且從該反應裝置!Q之出σ14排放出來的 時間大約為2 4 - 9 6小時。在本發明之中,由於黏結劑 之快速凝固的特性,因而使得在其他發明中所使用之熟化 方法的預先乾燥順序變得不需要。也因此降低了在小丸化 製程期間所發生之小丸的水不均勻性,亦即確保水合作用 與碳酸化作用的均勻性。 該小丸亦可在空氣中超過大約2 〇它的溫度下進行自 然熟化,而無須放置於直接陽光下大約1 4 一 2 8天。這 些小丸將具有一冷壓縮強度,正常情形下為大約2 5〜5 〇 kgf/小丸。這些小丸可以用於具有較低小丸強度需求 的製造’諸如在旋轉式爐床熔爐中的DRI製造。 相較於現有的技術:,,這些冷結合小丸及其製造方法具 有下列特徵: ^ 1 )該小丸具有足夠的冷壓縮強度;藉由該方法以包 含二氧化碳之熱氣體所熟化9 6小時的小丸將具有一冷壓 縮強度,正常情形下為大約7 8 _ 2 〇 〇 kgf/小丸,這 對於運輸和儲存而言是很適合的; 2 )該小丸將具有較高的熱強度,且不會在加熱和還 20 1302946 原期間裂解或粉碎,保值其固態形狀直到被熔化為止;軟 化/J2L的開始將會高於1000°C,並且可以加以調整; 3 )該小丸將具有一快的還原速度,如下: a )在900°C的環境溫度下歷時3小時,該還原程度 可以達到超過9 〇 % ;以及 b )在1200 C的環境溫度下歷時3 〇分鐘,幾乎所有 的鐵礦都會被還原; 、4 )包含煤或焦炭炭渣的小丸可以完全取代燒結物來 做為政風爐的進料,大幅降低焦炭對金屬的比例至大約2 δ 0 ν gf/1 ;該小丸亦可被用來做為非鼓風爐和dRI製造 中之製鐵的進料; 5)該小丸同樣可以做為直接製鋼之進料,大幅降低 製造成本; 6 )該小丸可以儲存报長的時間(超過1 〇年),而 不會粉碎; 7 )以相同的規格會需要相對低的投資資本,其係為 燒結物的二分之一或者是更少; 8 )在孩小丸之中可以使用所有種類之氧化鐵礦、製 鋼;於泥、以及包令童& s乳化鐵材料之滾軋銹垢;以及 )可以根據不同的熔化需求來調整該小丸之強度與 熔化特徵。 。亥小丸將會保持其原始結狗,如此可以避免其在高溫 的預熱環境和製鋼熔燐中 涮^合煻宁裂解和粉碎。藉由使用咼品質的 黏結劑、最理相 执 心勺a又计、以及特殊創造性之製造過程,該 21 1302946 一、 1強度之自動還原、冷結合的小丸可以在室溫和高溫 下被製造出來。在該熔渣與液態鐵分離之前,當該小丸被 加熱至一向溫的時候,該小丸將會保持其原始的形狀。 此特殊設計用於製鋼的小丸具有合理的内部含碳量。 所有芬與還原反應的材肖(鐵礦、煤粉末、和黏結劑), 二。 皮,、、、田地研磨並均勻地混合。特定面積可達到⑽2 -1二些所有的特徵將會提供該還原反應非常優異的動 悲反應條件。The better Vietnam; 4P (2) the volume of tricalcium phosphate and tricalcium aluminate should have a ratio between about 5 · 1 to 1 〇 · 1; (3) the cement clinker should be Finely cut so that the fraction of the particle size smaller than 0·08 mm should be about 90% or larger; (4) The free calcium oxide (f-CaO) content should be less than 3 wt%. 17 1302946 If the binder is less than about 1%, the pellet will have a low compressive strength' but if the binder is more than about 20%, it will also make the pellets relatively expensive to use. Under normal conditions, the binder content of the pellet falls between about 1 〇 2 〇 wt%. In some instances, an additive in the range of from about 0% to about 3% by weight may be added to the mash pellets. The additive may be composed of dolomite, limestone, lime, slaked lime, earthy soil, and any other material that can be adjusted, slag characteristics, and pellet strength. The size should be about 48 mesh or less. The composition of the pellet is about 6〇_79% by weight of iron ore concentrate, large, spoonful of 10 26 weights/G of carbon-containing reducing agent, and about weight%. Finely ground Portland cement clinker with special requirements, with a total weight of 100% 混合 mixed according to the weight ratio of the above-mentioned predetermined materials to create an isotropic mixture for the manufacture of pellets. The stomach mixture is formed into a "to-small pelletizing device, such as a spherical dish, or a rotating drum" to form pellets by adding sufficient water. Thereafter, the pellets are naturally matured in the line, or It is matured by an industrial maturation process, as described below. In the pelletization I, the pellets are sorted, such as by using a tromfiler to filter. This is because it is not necessary. The smaller or larger pellets of the crucible are separated and the loose powder adhered to the pellet is removed or adhered to the pellet more firmly. The purpose of eliminating or consolidating Xiaozhengzhi is to avoid When passing through the reaction device, 18 l3〇2946 J pills adhered to each other due to loose powder. After the lenght gentleman's extra number q and smaller or larger pellets can be recycled and again a. The normal condition of water contained in the raw pellets, ^, 舌 〇 / , Μ 备 在 大约 大约 大约 大约 大约 & & & & & & & & & & & & & & & & & & & & & & & & & & & & & & & & & & & & The top inlet acts in the 2 ❹reaction unit 1 Q to perform hydration, stone deacidification, and desiccation of the pellets. The individual vertical enthalpy is straight and has A n. The set of 10 is -" With the inlet 12 at its top, one out = the bottom 'and in a systematic manner divided into the upper half 6 people lower half 18 'the maturation gas is led to the reaction device + part 1 8 and in the upper half of the slot respectively After contact with the sputum pill, it is discharged from the inlet 12 of the trough. The reaction device 10 can have multiple inlets and outlets, if necessary. Most of the maturation gas is greater than (10) _ = Contains about 10 volumes of "higher carbon dioxide exhaust gas, and is from industrial furnaces, such as hot blast furnaces." " the pellets are sequentially and continuously passed through the reaction + part 1 6 and lower part 18 8. When advancing down to the upper half 16 6 , the pellets are slowly heated and come from the maturation gas from the lower half of the carbon dioxide The therapeutic gas evaporated by the pellets below is aged. When the pellets are advanced to the inside of the lower half of the reactor, the pellets will be heated and have about __ 3 〇〇 ° C The ripening gas containing carbon dioxide in the temperature range and the vapor evaporated from the pellets below are aged. In the route from the inlet 1 2 to the outlet i 4 of the reactor unit, 19 1302946, the pellets will be sequentially and continuously by main hydration, hydration and carbonation, mainly carbonation, and drying. (desiccati〇n) to ripen. Also, the pellets are sufficiently hydrated, carbonated, and dried. Once discharged from the reaction unit 1 , the pellets are ready for use. From the pellets from the inlet of the reaction unit i 丄 2 into the open = to the end 'and from the reaction device! The time that Q is discharged from σ14 is about 2 4 - 9 6 hours. In the present invention, the pre-drying order of the curing method used in other inventions becomes unnecessary due to the rapid solidification characteristics of the binder. It also reduces the water non-uniformity of the pellets that occur during the pelletization process, i.e., ensures uniformity of hydration and carbonation. The pellets can also be naturally aged in air at temperatures in excess of about 2 Torr, without being placed in direct sunlight for about 14 to 28 days. These pellets will have a cold compressive strength, normally about 2 5 to 5 〇 kgf per pellet. These pellets can be used in the manufacture of products having lower pellet strength requirements such as DRI fabrication in rotary hearth furnaces. Compared with the prior art: these cold-bonded pellets and their manufacturing method have the following characteristics: ^ 1) The pellet has sufficient cold compressive strength; the pellet is matured by a hot gas containing carbon dioxide by the method for 96 hours. Will have a cold compressive strength, normally about 7 8 _ 2 〇〇 kgf / pellet, which is very suitable for transportation and storage; 2) the pellet will have higher heat strength, and will not Heating and also 20 1302946 original period cracking or pulverizing, maintaining its solid shape until it is melted; softening / J2L will start higher than 1000 ° C, and can be adjusted; 3) the pellet will have a fast reduction rate, As follows: a) at a temperature of 900 ° C for 3 hours, the degree of reduction can reach more than 9 〇%; and b) at 1200 C ambient temperature for 3 〇 minutes, almost all iron ore will be reduced; 4) Pellets containing coal or coke carbon slag can completely replace the sinter as a feed for the gentamic furnace, greatly reducing the ratio of coke to metal to about 2 δ 0 ν gf / 1; the pellet can also be used As Non-blast furnace and feedstock for ironmaking in dRI manufacturing; 5) The pellet can also be used as a direct steel feed to significantly reduce manufacturing costs; 6) the pellet can store the length of the report (more than 1 year), and Will not smash; 7) Will require relatively low investment capital in the same specification, which is one-half or less of the sinter; 8) All kinds of iron oxide ore, steel can be used in the children's pellets ; in the mud, and the baking rust of the emulsified iron material; and) the strength and melting characteristics of the pellet can be adjusted according to different melting requirements. . Haixiaowan will maintain its original knot dog, so as to avoid its cracking and pulverization in the high temperature preheating environment and steel melting smelting. The 21 1302946 one- and one-intensity auto-reduced, cold-bonded pellets can be manufactured at room temperature and high temperature by using a 咼 quality adhesive, the most practical, and a particularly creative manufacturing process. . Before the slag is separated from the liquid iron, the pellet will retain its original shape when the pellet is heated to a constant temperature. This specially designed pellet for steelmaking has a reasonable internal carbon content. All the materials of fen and reduction reaction (iron ore, coal powder, and binder), II. The skin, ground, and field are ground and uniformly mixed. A certain area can reach (10) 2 - 1 and all of the features will provide very good reaction conditions for the reduction reaction.
:該小丸被放置到熔融鋼材之中時,由於高溫的因素, 付'、丸内部中的碳會完全气各 v 躍,而還原速率會报言。刀子會移動的很活 曰、同 因此’在這此種類之小丸中的猶 礦,在高溫下進行預弁Λn,、-禋類之J丸中的鐵 還;fτ 4 17…小丸被熔化之後,該鐵礦的 遇原均τ在不超過於的3分鐘内完成。 總結,因為所使用之 法,使得該自動還原、冷結:之::及製造該小丸的方 之熔化製程的需求。 、可以達到大部分形式: When the pellet is placed in molten steel, due to the high temperature factor, the carbon in the interior of the pellet will be completely vented, and the rate of reduction will be reported. The knife will move very lively, and therefore the 'mineral mine in this kind of pellet, pre-twisted at high temperature, the iron in the J-pill of the scorpion; fτ 4 17...the pellet is melted The iron ore's original τ is completed within 3 minutes of no more than 3 minutes. To sum up, because of the method used, the automatic reduction, cold junction:: and the requirements of the melting process for manufacturing the pellets. Can reach most forms
以下將以非限定之實施例 【實施方式】 凡月本發明。 實施例1 在製造出一混合物包括6 旦。、 重量%的無煙烊、 里%的鐵碌精砂、2 〇 以及1 3重量% Μ # 合物放置到一球狀碟盤中,米7、的黏結劑之後,將該混 造出具有大約9至! n D/ ;水添加至該混合物裡,以製 丄丄%之溼度含旦 再使用滾筒篩將該小 里的球狀小丸。之後, ]丸進仃分類’以製造出具有8 —16 22 1302946 mm之尺寸的小丸,然後再以本發明之方法將該小丸進行 熟化’其係於1 5 〇。。的溫度下利用熱的鼓風爐窯來進 行,並且包含大約2 5體積%的二氧化碳,歷時大約Q 6 小時。該乾燥之小丸的主要化學組成如下(以重量計之): TFe* Ca〇 Si〇2 a12〇3 Mg〇 C** 45.5 8·3 7·〇 2 · 5 3 · 3 1 4 · 2The following are non-limiting examples. [Embodiment] Example 1 A mixture was made to include 6 denier. , wt% of smokeless sputum, 5% of iron sinter, 2 〇, and 13% by weight of Μ# compound placed in a spherical disk, after the binder of rice 7, the mixture has a 9 to! n D/; water is added to the mixture to make the sputum of the sputum, and the spheroid pellets of the spheroid are used. Thereafter, the pellets were sorted to produce pellets having a size of 8-16 22 1302946 mm, and then the pellets were aged by the method of the present invention, which was tied at 15 Torr. . The temperature is measured using a hot blast furnace and contains approximately 25 vol% carbon dioxide for approximately 6 hours. The main chemical composition of the dried pellets is as follows (by weight): TFe* Ca〇 Si〇2 a12〇3 Mg〇 C** 45.5 8·3 7·〇 2 · 5 3 · 3 1 4 · 2
冷壓縮強度為8 0 kgf//小丸。軟化溫度的起始為 7 0 °C。可以將該小丸用於較小的鼓風爐、和腿溶爐 或者是其他應用中做為製鐵的進料。 實施例The cold compressive strength is 80 kgf// pellet. The softening temperature starts at 70 °C. The pellets can be used in smaller blast furnaces, and in leg ovens or in other applications as feedstock for ironmaking. Example
使用相同於實施例1中 成分’成為75重量%的鐵 渣、以及1 2重量%的黏結 小丸之強度將會增加。該經 下(以重量計之)·· 的方法,但是改變該混合物的 礦精砂、1 3重量%的焦炭炭 劑,相較於實施例1而言,該 熟化之小丸的主要化學組成如 q * * 10-66 TFe* Ca0 Si〇2 Al2〇3 Mg〇 50·68 8·37 6·36 1·87 1·68 冷壓縮強度為1 〇 〇 kgf/小丸。軟化溫度的起始為工 f 〇 〇t °可以將該小丸取代燒結物來做為大型鼓風爐的 ’裁進料,且其將會降低焦炭的消耗,以每噸生鐵之2 3 8公斤。 ' 23 1302946 另一個實施例之小丸主要的化學組成如下(以重量呀 之)·· s °The strength of using 75% by weight of iron slag and 12% by weight of the bonded pellets in the same manner as in Example 1 will increase. The method of the following (by weight), but changing the mineral concentrate of the mixture, 13% by weight of the coke charge, compared to Example 1, the main chemical composition of the cooked pellets is q * * 10-66 TFe* Ca0 Si〇2 Al2〇3 Mg〇50·68 8·37 6·36 1·87 1·68 The cold compressive strength is 1 〇〇kgf/ pellet. The softening temperature starts with the work f 〇 〇t °. The pellet can be used instead of the sinter to make a cut into the large blast furnace, and it will reduce the consumption of coke to 238 kg per ton of pig iron. ' 23 1302946 The main chemical composition of the pellet of another embodiment is as follows (by weight)·· s °
C a〇 S i 〇2 A 1 2〇3 Mg〇 Q * * 7 · 6 6 · 1 2 · 〇 0 · 6 8 · 6 8 · 3 6 · 8 2 · 2 0 · 9 10· 總合F e 固定C TF e * 4 9 · 5 4 9 · 1 氺 氺C a〇S i 〇2 A 1 2〇3 Mg〇Q * * 7 · 6 6 · 1 2 · 〇0 · 6 8 · 6 8 · 3 6 · 8 2 · 2 0 · 9 10 · Total F e Fixed C TF e * 4 9 · 5 4 9 · 1 氺氺
本發明之規則、較佳具體態樣、以及操作模式均以於 之丽的說明書中加以敘述。然而,本發明所欲請求保護的 並非受限於特定所揭示的具體態樣中。該具體態樣應該被 視為說明性質而非限制範圍性質。在不背離本發明之精神 2範疇的情形下均可進行各種不同的變化與修正。因此, ;本么明之精神與範疇之所有這些各種不同的變化與修 如同以下之申請專利範圍中所定義,明顯均為需要包 括的。The rules, preferred aspects, and modes of operation of the invention are set forth in the description of the invention. However, the invention is not intended to be limited to the particular embodiments disclosed. This specific aspect should be considered as illustrative rather than limiting. Various changes and modifications can be made without departing from the spirit of the invention. Therefore, all of the various changes and modifications of the spirit and scope of the present invention are obviously as defined in the following claims.
【圖式簡單說明】 圖1係為說明本發明纟置之具體態樣的概要圖。 【主要元件符號說明】 ίο.反應裝置 1 2 ·入口 14·出口 16·上部分 1 8 ·下部分 24BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a schematic view showing a specific aspect of the apparatus of the present invention. [Explanation of main component symbols] ίο.Reaction device 1 2 ·Inlet 14·Exit 16·Upper part 1 8 ·Lower part 24
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW93127993A TWI302946B (en) | 2004-09-16 | 2004-09-16 | Self-reducing, cold-bonded pellets |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW93127993A TWI302946B (en) | 2004-09-16 | 2004-09-16 | Self-reducing, cold-bonded pellets |
Publications (1)
Publication Number | Publication Date |
---|---|
TWI302946B true TWI302946B (en) | 2008-11-11 |
Family
ID=45070590
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW93127993A TWI302946B (en) | 2004-09-16 | 2004-09-16 | Self-reducing, cold-bonded pellets |
Country Status (1)
Country | Link |
---|---|
TW (1) | TWI302946B (en) |
-
2004
- 2004-09-16 TW TW93127993A patent/TWI302946B/en active
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR101158883B1 (en) | Self-reducing, cold-bonded pellets | |
TWI237061B (en) | Process for producing particulate iron metal | |
JP4627236B2 (en) | Manufacturing method of carbonized material agglomerates | |
CN102482730A (en) | Unfired carbon-containing agglomerate for blast furnaces and production method therefor | |
EA023830B1 (en) | Method for producing an agglomerate made of fine material containing metal oxide for use as a blast furnace feed material | |
BRPI0920547A2 (en) | method for operating blast furnace using uncooked pellets containing coal. | |
RU2458158C2 (en) | Method of obtaining pelletised metallurgical raw materials | |
CN106414778A (en) | Production method of granular metallic iron | |
JP5512205B2 (en) | Strength improvement method of raw material for agglomerated blast furnace | |
JP3502011B2 (en) | Manufacturing method of carbonized interior agglomerates | |
JP2009161791A5 (en) | ||
TWI302946B (en) | Self-reducing, cold-bonded pellets | |
JP6992644B2 (en) | Method for producing uncalcined agglomerate for blast furnace and method for producing pozzolan-reactive iron-containing raw material | |
JP5454505B2 (en) | Method for producing unfired carbon-containing agglomerated blast furnace | |
JPS60248831A (en) | Manufacture of uncalcined lump ore | |
JP2011032532A (en) | Method for producing agglomerate for blast furnace raw material | |
JPS61178449A (en) | Use of steel slag | |
JPS61163221A (en) | Manufacture of nonsintered type briquetted ore | |
JPS6227527A (en) | Method for utilizing desiliconization slag | |
JP2005290525A (en) | Method for producing cold-agglomerated ore for blast furnace | |
RU2430979C2 (en) | Procedure for preparation of charge for manufacture of metallised product | |
JP2009019241A (en) | Method for operating blast furnace using non-fired agglomerated ore | |
JPS61178450A (en) | Use of steel slag | |
JPH0621301B2 (en) | Sintering method of iron ore | |
JPS6227528A (en) | Utilizing method for desiliconized slag |