TWI523952B - The preparation method of modified converter slag - Google Patents
The preparation method of modified converter slag Download PDFInfo
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- TWI523952B TWI523952B TW103113031A TW103113031A TWI523952B TW I523952 B TWI523952 B TW I523952B TW 103113031 A TW103113031 A TW 103113031A TW 103113031 A TW103113031 A TW 103113031A TW I523952 B TWI523952 B TW I523952B
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Description
本發明是有關於一種轉爐石渣的製備方法,特別是指一種經改質轉爐石渣的製備方法。 The invention relates to a preparation method of converter stone slag, in particular to a preparation method of modified converter stone slag.
爐石為煉鋼之副產品,一般依製程可分為高爐石與轉爐石兩種。高爐石粉已被廣泛應用於水泥混凝土中,但轉爐石渣因成分中含有大量活性氧化物(如氧化鈣),易與水發生反應,使轉爐石渣體積膨脹產生變化,故以往均將轉爐石渣視為煉鋼固態廢棄物。 Hearthstone is a by-product of steelmaking. Generally, it can be divided into two types: blast furnace stone and converter stone. Blast furnace stone powder has been widely used in cement concrete, but the converter stone slag contains a large amount of active oxides (such as calcium oxide), which easily reacts with water, which causes the volume expansion of converter slag to change, so in the past, converter stone Slag is considered as solid waste in steel making.
然而,在上述改質方法中,由於轉爐石渣中FeO含量有限,無法提供大量熱源來升溫以讓轉爐石渣維持於液態渣狀態,且於吹入矽砂時亦會產生降溫作用,因此於改質時,轉爐石渣易因降溫產生固化而無法繼續進行改質,導致轉爐石渣的改質成功率降低,使轉爐石渣不能再被利用,造成大量廢棄物產生並汙染環境。 However, in the above modification method, since the content of FeO in the converter slag is limited, a large amount of heat source cannot be supplied to raise the temperature to maintain the converter slag in a liquid slag state, and a cooling effect is also generated when the blasting sand is blown, so When the product is upgraded, the converter stone slag is easy to be solidified due to cooling, and the reforming success rate of the converter stone slag is reduced, so that the converter stone slag can no longer be used, causing a large amount of waste to be generated and polluting the environment.
鑒於習知方法於改質轉爐石渣時易因熱源不足造成降溫固化而無法繼續進行改質的缺點,本案發明人首先思及於吹入氧氣前加入含鋁金屬之材料於轉爐石渣中,透過含鋁金屬之材料中的鋁金屬和吹入的氧氣反應產生氧 化鋁時所放出的熱能作為熱源來提升轉爐石渣於改質過程中的溫度,使轉爐石渣能長時間維持於液態渣狀態,以補償習知方法於改質時熱源不足的問題。 In view of the shortcomings of the conventional method for upgrading the converter stone slag, which is easy to be cooled and solidified due to insufficient heat source, and the reform cannot be continued, the inventor of the present invention first considers adding the material containing aluminum metal to the converter stone slag before blowing oxygen. Producing oxygen by reacting aluminum metal in a material containing aluminum metal with oxygen blown in The heat energy released during the aluminum is used as a heat source to raise the temperature of the converter stone slag during the upgrading process, so that the converter stone slag can be maintained in the liquid slag state for a long time, so as to compensate for the problem of insufficient heat source in the conventional method.
因此,本發明之目的,即在提供一種於改質過程中,轉爐石渣不易因熱源不足造成降溫固化之經改質轉爐石渣的製備方法。 Therefore, the object of the present invention is to provide a method for preparing a modified converter stone slag which is not easily cooled and solidified due to insufficient heat source during the upgrading process.
於是本發明經改質轉爐石渣的製備方法包含下列步驟:(1)將含鋁金屬之材料加入液態轉爐石渣中,得到一含鋁轉爐石渣;(2)於該含鋁轉爐石渣中吹入氧氣後,進行升溫,得到一經升溫轉爐石渣;及(3)於該經升溫轉爐石渣中吹入矽砂進行改質,得到一經改質轉爐石渣。 Therefore, the method for preparing the modified converter stone slag of the present invention comprises the following steps: (1) adding a material containing aluminum metal to the liquid converter stone slag to obtain an aluminum-containing converter stone slag; and (2) forming the aluminum-containing converter stone slag After the oxygen is blown into the middle, the temperature is raised to obtain a temperature-returning stone slag; and (3) the blasted sand is blown into the temperature-controlled converter stone slag to be modified to obtain a modified converter stone slag.
本發明之功效是於轉爐石渣改質過程中,將含鋁金屬之材料加入液態轉爐石渣內,並藉由鋁金屬和氧氣反應產生熱能作為熱源,使轉爐石渣不易因熱源不足造成降溫固化而導致改質失敗,因此提升轉爐石渣的改質成功率。 The effect of the invention is that in the process of upgrading the converter stone slag, the material containing aluminum metal is added into the liquid converter stone slag, and the heat energy generated by the reaction of aluminum metal and oxygen is used as a heat source, so that the converter stone slag is not easily cooled due to insufficient heat source. Curing causes the upgrading to fail, thus improving the success rate of the converter gravel.
以下將就本發明內容進行詳細說明:該步驟(1)的含鋁金屬之材料可為任何含有鋁金屬並適用於改質轉爐石渣之材料,較佳地,該含鋁金屬之材料為鋁製業廢棄物中的鋁渣,如鋁業熔煉作業中產出之鋁渣。 The invention will be described in detail below. The aluminum-containing metal material of the step (1) may be any material containing aluminum metal and suitable for upgrading the converter stone slag. Preferably, the aluminum-containing metal material is aluminum. Aluminium slag in industrial waste, such as aluminum slag produced in aluminum smelting operations.
較佳地,該鋁渣與該轉爐石渣重量比範圍為1:15~1:120。更佳地,該鋁渣與該轉爐石渣重量比為1:40。 Preferably, the weight ratio of the aluminum slag to the converter gravel ranges from 1:15 to 1:120. More preferably, the weight ratio of the aluminum slag to the converter gravel is 1:40.
較佳地,該鋁渣含有15~25wt%鋁金屬。 Preferably, the aluminum slag contains 15 to 25 wt% of aluminum metal.
較佳地,步驟(2)是藉由該含鋁金屬之材料中的鋁金屬和氧氣反應所產生的熱能來進行升溫,其反應如下式(I)所示:4Al+3O2 → 2Al2O3+熱能 (I) Preferably, the step (2) is carried out by the thermal energy generated by the reaction of the aluminum metal and the oxygen in the aluminum-containing metal material, and the reaction is as shown in the following formula (I): 4Al+3O 2 → 2Al 2 O 3 + heat (I)
較佳地,該轉爐石渣含有氧化亞鐵,且步驟(2)還藉由氧化亞鐵和氧氣反應所產生的熱能來進行升溫,其反應如下式(II)所示:2FeO+1/2O2 → Fe2O3+熱能 (II) Preferably, the converter stone slag contains ferrous oxide, and step (2) is further heated by the heat energy generated by the reaction of ferrous oxide and oxygen, and the reaction is as shown in the following formula (II): 2FeO+1/2O 2 → Fe 2 O 3 + thermal energy (II)
較佳地,步驟(2)之經升溫轉爐石渣的操作溫度範圍為1380℃~1530℃。 Preferably, the operating temperature range of the temperature-increasing converter gravel in step (2) is from 1380 ° C to 1530 ° C.
於步驟(3)中,當該經升溫轉爐石渣中吹入矽砂後,是藉由轉爐石渣中的CaO和矽砂反應產生矽酸鹽化合物來改質轉爐石渣,其反應如下式(III)所示:2CaO+SiO2 → 2CaO.SiO2 (III) In the step (3), after the blast furnace is blown into the temperature-refined converter stone slag, the converter slag is modified by reacting CaO and strontium in the converter slag to react the slag compound, and the reaction is as follows (III): 2CaO + SiO 2 → 2CaO. SiO 2 (III)
於步驟(3)中,轉爐石渣中的CaO還會藉由和氧化亞鐵與氧氣反應後所產生的氧化鐵進行反應來改質轉爐石渣,其反應如下式(IV)和所示:2CaO+Fe2O3 → 2CaO.Fe2O3 (IV) In the step (3), the CaO in the converter stone slag is further modified by the iron oxide produced by the reaction between the ferrous oxide and the oxygen, and the reaction is as follows: (IV) and shown: 2CaO+Fe 2 O 3 → 2CaO. Fe 2 O 3 (IV)
本發明將就以下實施例來作進一步說明,但應瞭解的是,該實施例僅為例示說明之用,而不應被解釋為本發明實施之限制。 The present invention will be further illustrated by the following examples, but it should be understood that this embodiment is intended to be illustrative only and not to be construed as limiting.
步驟(1):將鋁製業廢棄物中的鋁渣(成分如下表1所示)加入操作溫度為1380~1530℃之欲改質且為液態的轉爐石渣中(鋁渣:轉爐石渣重量比為1:40),獲得含鋁轉爐石渣。 Step (1): Adding aluminum slag in the aluminum industry waste (the composition is as shown in Table 1 below) to the converter slag to be upgraded and liquid at an operating temperature of 1380 to 1530 ° C (aluminum slag: converter slag) The weight ratio is 1:40), and an aluminum-containing converter stone residue is obtained.
步驟(2):將該吹氧管插入步驟(1)所得且尚處於液態的含鋁轉爐石渣中,吹入約70~120m3氧氣(吹射時間約20~35分),使該鋁渣中的鋁金屬及該轉爐石渣中的氧化亞鐵分別和氧氣反應,以各自產生氧化鋁、氧化鐵及熱能,並以該二反應所產生的熱能作為熱源,使該含鋁轉爐石渣升溫至1450~1530℃後,獲得經升溫轉爐石渣。 Step (2): inserting the oxygen lance into the aluminum-containing converter slag which is obtained in the step (1) and is still in a liquid state, blowing about 70-120 m 3 of oxygen (the blowing time is about 20-35 minutes), so that the aluminum is made. The aluminum metal in the slag and the ferrous oxide in the converter stone slag react with oxygen to generate alumina, iron oxide and heat energy, respectively, and use the heat energy generated by the two reactions as a heat source to make the aluminum-containing converter stone residue After the temperature is raised to 1450~1530 °C, the temperature-controlled converter stone residue is obtained.
步驟(3):將該步驟(2)所得經升溫轉爐石渣吹入2.4~4.0噸矽砂(SiO2)(吹射時間約20~35分),使該矽砂受熱溶解,此時,於轉爐石渣中的CaO會和矽砂反應生成矽酸鹽化合物(2CaO.SiO2)進行改質,或CaO會和步驟(2)中所產生的氧化鐵反應生成2CaO.Fe2O3進行改質,因而獲得經改質轉爐石渣。 Step (3): blowing the heated furnace slag obtained in the step (2) into 2.4 to 4.0 tons of cerium (SiO 2 ) (blowing time of about 20 to 35 minutes), so that the cerium is dissolved by heat, at this time, The CaO in the converter stone slag reacts with the cerium to form a phthalate compound (2CaO.SiO 2 ) for modification, or CaO reacts with the iron oxide produced in the step (2) to form 2CaO. The Fe 2 O 3 is modified to obtain a modified converter stone residue.
依據實施例1的製備方法,在101年10月1日至12月31日,分別對吹射一站及吹射二站中的轉爐石渣進行改質,接著分別統計總處理桶數,以及於吹射矽砂時因熱源不足造成降溫固化,而無法進行轉爐石渣改質的爐次(即,固化桶數),結果整理於表2中。 According to the preparation method of the first embodiment, the converter stone slag in the one station of the blowing and the second station of the blowing is respectively modified from October 1 to December 31, 101, and then the total number of barrels is counted separately, and When the blasting sand was blown, the heat was cooled due to insufficient heat source, and the heat of the converter slag was not able to be reformed (that is, the number of solidified barrels). The results are summarized in Table 2.
另於102年1月1日至7月30日,依據實施例2的製備方法分別對吹射一站及吹射二站中的轉爐石渣進行改質,同樣統計無法進行轉爐石渣改質的固化桶數,結果整理於表2中。 In addition, from January 1 to July 30, 102, according to the preparation method of Example 2, the converter slag in the one station of the blowing and the two stations in the blowing station were respectively modified, and the conversion of the converter slag could not be performed. The number of curing barrels is shown in Table 2.
分別依據實施例1之製備方法中的步驟(2)及(3)[也就是未進行步驟(1)],分別對吹射一站及吹射二站中的轉爐石渣進行改質,接著分別統計總處理桶數,以及於吹射矽砂時因熱源不足造成降溫固化,而無法進行轉爐石 渣改質的固化桶數,結果整理於表2中。 According to steps (2) and (3) in the preparation method of Example 1, respectively, that is, step (1) is not performed, respectively, the converter stone slag in the one-stop and two-blowing stations is modified, and then The total number of barrels is counted separately, and when the sand is blown, the heat is cooled due to insufficient heat source, and the converter stone cannot be used. The number of solidified barrels modified by slag was compiled in Table 2.
由表2顯示,若於吹射氧氣前加入鋁渣於轉爐石渣中,其固化比率會由22.72%(未加鋁渣)大幅降至2.97%,證實本發明製備方法,利用鋁渣中的鋁金屬和吹入的氧氣反應產生熱能作為熱源來提升改質時轉爐石渣溫度,使其長時間能維持於液態渣狀態,確實有效改善習知方法於改質時因熱源不足所造成之轉爐石渣降溫固化而無法進行改質的問題。 Table 2 shows that if aluminum slag is added to the converter slag before blowing oxygen, the curing ratio will be greatly reduced from 22.72% (without adding aluminum slag) to 2.97%, confirming the preparation method of the present invention, using aluminum slag The aluminum metal reacts with the blown oxygen to generate heat as a heat source to improve the temperature of the converter slag during the upgrading, so that it can be maintained in the state of liquid slag for a long time, and it is indeed effective to improve the converter caused by insufficient heat source in the conventional method. The problem is that the gravel is cooled and solidified and cannot be upgraded.
綜上所述,本發明經改質轉爐石渣的製備方法是於轉爐石渣改質過程中,藉由將含鋁金屬之材料加入液態轉爐石渣內,使轉爐石渣不易因熱源不足造成降溫固化而導致改質失敗,因此提升轉爐石渣改質成功率,故確實能達成本發明之目的。 In summary, the modified converter grate of the present invention is prepared by adding the aluminum-containing metal material into the liquid converter stone slag during the upgrading process of the converter stone slag, so that the converter stone slag is not easily caused by insufficient heat source. The cooling and solidification causes the upgrading to fail, so that the success rate of the converter gravel upgrading is improved, so the object of the present invention can be achieved.
惟以上所述者,僅為本發明之較佳實施例而已,當不能以此限定本發明實施之範圍,即大凡依本發明申請專利範圍及專利說明書內容所作之簡單的等效變化與修飾,皆仍屬本發明專利涵蓋之範圍內。 The above is only the preferred embodiment of the present invention, and the scope of the present invention is not limited thereto, that is, the simple equivalent changes and modifications made by the patent application scope and patent specification content of the present invention, All remain within the scope of the invention patent.
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