TW201808855A - Method of manufacturing binder material, cured mortar and cured mortar forming by thereof - Google Patents

Method of manufacturing binder material, cured mortar and cured mortar forming by thereof Download PDF

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TW201808855A
TW201808855A TW105129807A TW105129807A TW201808855A TW 201808855 A TW201808855 A TW 201808855A TW 105129807 A TW105129807 A TW 105129807A TW 105129807 A TW105129807 A TW 105129807A TW 201808855 A TW201808855 A TW 201808855A
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mortar
steel
making slag
alkaline solution
manufacturing
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TW105129807A
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TWI682916B (en
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黃忠信
陳泰安
林孟佑
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國立成功大學
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Priority to CN201710377145.7A priority patent/CN107814497A/en
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    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B7/00Hydraulic cements
    • C04B7/14Cements containing slag
    • C04B7/147Metallurgical slag
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B28/00Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
    • C04B28/02Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements containing hydraulic cements other than calcium sulfates
    • C04B28/08Slag cements
    • C04B28/082Steelmaking slags; Converter slags
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/10Production of cement, e.g. improving or optimising the production methods; Cement grinding

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Inorganic Chemistry (AREA)
  • Processing Of Solid Wastes (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)

Abstract

Method of manufacturing binder material, cured mortar and cured mortar forming by thereof are provided. Steps of the method of manufacturing binders are stated as follows. Steelworks slags are provided. The steelworks slags are immersed in water to form an alkaline solution. The steelworks slags are separated from the alkaline solution. Glass powder is added in the alkaline solution to form a binder solution. The binder solution is cured to form a binder material.

Description

膠結材、砂漿固化物的製造方法及藉由其所形成的砂漿固化物Method for manufacturing cementitious material, mortar cured product, and mortar cured product formed thereby

本發明是有關於一種混凝土材料及其製造方法,且特別是有關於一種膠結材、砂漿固化物的製造方法及藉由其所形成的砂漿固化物。The present invention relates to a concrete material and a method for manufacturing the same, and particularly relates to a method for manufacturing a cemented material and a cured mortar and a cured mortar formed therefrom.

煉鋼爐渣為煉製鋼鐵時所產生的副產物,其形成的方式為煉鋼原料在高爐裡經熔煉後,產生的雜質經過氧化與金屬分離或燃燒後所形成的渣滓等,然而,若不對煉鋼爐渣加以回收再利用,不僅會讓煉鋼業者需額外負擔處理煉鋼爐渣的費用,也會造成環境的負擔。Steel-making slag is a by-product produced during steelmaking. It is formed by smelting steel-making raw materials in a blast furnace. The resulting impurities are separated from the metal by oxidation or slag formed after combustion or combustion. However, if it is not correct The recycling and reuse of steel-making slag will not only cause the steel-making industry to pay extra for the cost of processing the steel-making slag, but also cause a burden on the environment.

早期為藉由掩埋的方式來處理煉鋼爐渣,然而,其會使環境受到煉鋼爐渣中的重金屬的汙染。而隨著工業技術的發展,煉鋼爐渣可經安定化處理(stabilizing treatment)後再將其添加於各式建築物的土木材料中,然而,煉鋼爐渣在吸水或接觸空氣中的二氧化碳之後,其會膨脹而因此使建築物的結構強度降低,使得煉鋼爐渣回收再利用的範圍受到限制。因此,目前急需提供一種煉鋼爐渣之處理方法,以徹底解決習知技術中處理煉鋼爐渣的缺陷,以提升其產業利用性。In the early days, the steelmaking slag was treated by burying, however, it would make the environment polluted by heavy metals in the steelmaking slag. With the development of industrial technology, steelmaking slag can be added to the civil materials of various buildings after stabilizing treatment. However, after the steelmaking slag absorbs water or contacts carbon dioxide in the air, It will expand and thus reduce the structural strength of the building, which limits the scope of steelmaking slag recovery and reuse. Therefore, there is an urgent need to provide a method for treating steel-making slag in order to completely solve the defects in the treatment of steel-making slag in the conventional technology, so as to enhance its industrial utilization.

本發明提供一種膠結材的製造方法,其包括下列步驟:提供煉鋼爐渣;將煉鋼爐渣浸泡在水中,以使水形成鹼性溶液;將鹼性溶液與煉鋼爐渣分離;在鹼性溶液中加入玻璃粉末,以形成膠結溶液;以及固化膠結溶液,以形成膠結材。The invention provides a method for manufacturing a cement material, which includes the following steps: providing steel-making slag; soaking the steel-making slag in water to form an alkaline solution in the water; separating the alkaline solution from the steel-making slag; in the alkaline solution Glass powder is added to form a cementing solution; and the cementing solution is cured to form a cementitious material.

本發明提供一種砂漿固化物的製造方法,其包括下列步驟:提供煉鋼爐渣;將煉鋼爐渣浸泡在水中,以使水形成鹼性溶液;於含煉鋼爐渣的鹼性溶液中加入玻璃粉末並攪拌,以形成砂漿;以及固化砂漿,以形成砂漿固化物。The invention provides a method for manufacturing a solidified mortar, which includes the following steps: providing steel-making slag; soaking the steel-making slag in water to form an alkaline solution in the water; adding glass powder to the alkaline solution containing the steel-making slag And stirring to form a mortar; and curing mortar to form a mortar cured product.

本發明提供另一種砂漿固化物的製造方法,其包括下列步驟:提供煉鋼爐渣;將煉鋼爐渣浸泡在水中,以使水形成鹼性溶液;將鹼性溶液與煉鋼爐渣分離;於鹼性溶液中加入玻璃粉末及細粒料並攪拌,以形成砂漿;以及固化砂漿,以形成砂漿固化物。The present invention provides another method for manufacturing solidified mortar, which includes the following steps: providing steel-making slag; soaking the steel-making slag in water to form an alkaline solution in the water; separating the alkaline solution from the steel-making slag; Glass powder and fine particles are added to the sexual solution and stirred to form a mortar; and cured mortar to form a cured mortar.

本發明提供一種砂漿固化物,其包括10~50 wt%的煉鋼爐渣以及50~90 wt%的上述的膠結材。The invention provides a solidified mortar, which includes 10-50 wt% of steel-making slag and 50-90 wt% of the above-mentioned cementitious material.

基於上述,本發明的膠結材及砂漿固化物的製造方法將煉鋼爐渣及廢棄玻璃作為形成膠結材的原料之一,除可將煉鋼爐渣及廢棄玻璃回收再利用外,亦可使處理煉鋼爐渣及廢棄玻璃所需的成本與形成膠結材及砂漿固化物的原料成本降低。另外,本發明藉由將煉鋼爐渣浸泡在水中以形成鹼性溶液,藉由鹼性溶液中的氫氧根離子與玻璃粉末進行反應,因此,可不需額外購買鹼金屬或鹼土金屬之氫氧化物及矽酸鈉等來自備鹼性溶液,而使形成膠結材及砂漿固化物的原料成本降低。Based on the above, the manufacturing method of the cemented material and the mortar cured product of the present invention uses steelmaking slag and waste glass as one of the raw materials for forming the cementitious material. In addition to recycling the steelmaking slag and waste glass, it can also be processed The cost of steel slag and waste glass and the cost of raw materials to form cement and mortar solidification are reduced. In addition, by soaking the steel-making slag in water to form an alkaline solution, the hydroxide ions in the alkaline solution react with the glass powder, so there is no need to purchase additional alkali metal or alkaline earth metal hydroxide The raw materials and sodium silicate come from the preparation of alkaline solution, which reduces the cost of raw materials for forming cement and mortar cured products.

為讓本發明的上述特徵和優點能更明顯易懂,下文特舉實施例,並配合所附圖式作詳細說明如下。In order to make the above-mentioned features and advantages of the present invention more obvious and understandable, the embodiments are specifically described below and described in detail in conjunction with the accompanying drawings.

圖1為本發明的一實施例的膠結材的製造方法的步驟流程圖。FIG. 1 is a flowchart of steps of a method for manufacturing a cement material according to an embodiment of the invention.

請參照圖1,在步驟S100中,提供煉鋼爐渣。煉鋼爐渣的來源主要為在煉鋼時產生的副產品,舉例來說,煉鋼爐渣可包括轉爐石(basic-oxygen-furnace slag;BOF)或電弧爐渣(electric-arc-furnace slag;EAF)等。在本實施例中,煉鋼爐渣可為轉爐石或電弧爐渣。由於煉鋼爐渣可作為後續形成砂漿或混凝土中的細粒料之用途來使用,因此煉鋼爐渣的粒徑會接近一般土木領域裡常用的細粒料的粒徑。在本實施例中,煉鋼爐渣的粒徑小於4.75 mm。Referring to FIG. 1, in step S100, steel-making slag is provided. The sources of steel-making slag are mainly by-products produced during steel-making. For example, steel-making slag may include converter-stone (basic-oxygen-furnace slag; BOF) or electric-arc-furnace slag (EAF), etc. . In this embodiment, the steel-making slag may be converter stone or electric arc slag. Since the steel-making slag can be used for the subsequent formation of fine particles in mortar or concrete, the particle size of the steel-making slag will be close to the particle size of fine particles commonly used in the general civil engineering field. In this embodiment, the particle size of the steel-making slag is less than 4.75 mm.

接著,在步驟S110中,將煉鋼爐渣浸泡在水中,以使水形成鹼性溶液。由於煉鋼爐渣含有大量來自於煉鋼時添加的石灰石中的游離氧化鈣(free-CaO),因此,當將煉鋼爐渣浸泡在水中時,游離氧化鈣溶於水而形成氫氧化鈣,並於水中解離出氫氧根離子,使得水的pH值上升而形成鹼性溶液。煉鋼爐渣的浸泡溫度會影響氫氧化鈣於水中解離出的氫氧根離子的量,如表1所示,當煉鋼爐渣的浸泡溫度越低時,氫氧化鈣於水中解離出的氫氧根離子的量越多,而使鹼性溶液的pH值越高。在本實施例中,煉鋼爐渣於水中的浸泡溫度為0°C~90°C,較佳為0°C~25°C,更佳為接近0°C。在本實施例中,鹼性溶液的pH值範圍為11~13。本實施例藉由將煉鋼爐渣浸泡在水中使水形成鹼性溶液,不需額外購買鹼金屬或鹼土金屬之氫氧化物及矽酸鈉等來自備鹼性溶液,因此可降低所需的原料成本。Next, in step S110, the steel-making slag is immersed in water so that the water forms an alkaline solution. Since the steel-making slag contains a large amount of free calcium oxide (free-CaO) from limestone added during steel-making, when the steel-making slag is immersed in water, the free calcium oxide dissolves in water to form calcium hydroxide, and The hydroxide ions are dissociated in water, causing the pH of the water to rise to form an alkaline solution. The immersion temperature of steel-making slag will affect the amount of hydroxide ions dissociated from calcium hydroxide in water. As shown in Table 1, when the immersion temperature of steel-making slag is lower, the hydroxide of calcium hydroxide dissociated from water The greater the amount of root ions, the higher the pH of the alkaline solution. In this embodiment, the immersion temperature of the steel-making slag in water is 0 ° C to 90 ° C, preferably 0 ° C to 25 ° C, and more preferably close to 0 ° C. In this embodiment, the pH value of the alkaline solution ranges from 11 to 13. In this embodiment, the steel-making slag is immersed in water to form an alkaline solution. There is no need to purchase additional alkali metal or alkaline earth metal hydroxides and sodium silicate etc. from the preparation of alkaline solution, so the required raw materials can be reduced cost.

表1 Table 1

另外,鹼性溶液中的水與煉鋼爐渣的重量比例也會影響鹼性溶液的pH值,在本實施例中,煉鋼爐渣可為轉爐石或電弧爐渣,因此,於此處以水與轉爐石(W/BOF)的重量比例為例。如表2所示,當W/BOF越小,意即鹼性溶液中的轉爐石越多,而使鹼性溶液含有較多的氫氧化鈣,因此,鹼性溶液中的pH值越高;相對地,當W/BOF越大,意即鹼性溶液中的轉爐石越少,而使鹼性溶液含有較少的氫氧化鈣,因此,鹼性溶液中的pH值越低。在本實施例中,W/BOF的範圍為0.25~2.0。W/BOF在此範圍內時,可確保鹼性溶液中含有足夠的氫氧根離子。In addition, the weight ratio of water in the alkaline solution to the steel-making slag will also affect the pH of the alkaline solution. In this embodiment, the steel-making slag may be converter stone or electric arc slag. Therefore, water and converter are used here Take the weight ratio of stone (W / BOF) as an example. As shown in Table 2, the smaller the W / BOF, the more converter stones in the alkaline solution, and the alkaline solution contains more calcium hydroxide. Therefore, the higher the pH value in the alkaline solution; relative Ground, when W / BOF is larger, it means that there is less converter stone in the alkaline solution, and the alkaline solution contains less calcium hydroxide, therefore, the lower the pH value in the alkaline solution. In this embodiment, the range of W / BOF is 0.25 to 2.0. When the W / BOF is within this range, it can ensure that the alkaline solution contains enough hydroxide ions.

表2 Table 2

再來,在步驟S120中,將鹼性溶液與煉鋼爐渣分離。當煉鋼爐渣於水中浸泡一定時間後,氫氧化鈣於水中解離出的氫氧根離子的量已達飽和,意即,鹼性溶液的pH值已達平衡。在本實施例中,煉鋼爐渣於水中的浸泡時間為1~48小時,較佳為12~48小時,更佳為24小時。當鹼性溶液的pH值達平衡時,可將煉鋼爐渣自鹼性溶液中分離出。將煉鋼爐渣自鹼性溶液中分離出的方法可例如是藉由濾網過濾出鹼性溶液中的煉鋼爐渣,但於本實施例中其並沒有特別的限制。Next, in step S120, the alkaline solution and the steel-making slag are separated. After the steel-making slag is immersed in water for a certain period of time, the amount of hydroxide ions dissociated from the calcium hydroxide in the water has reached saturation, which means that the pH value of the alkaline solution has reached equilibrium. In this embodiment, the immersion time of the steel-making slag in water is 1 to 48 hours, preferably 12 to 48 hours, and more preferably 24 hours. When the pH value of the alkaline solution reaches equilibrium, the steel-making slag can be separated from the alkaline solution. The method for separating the steel-making slag from the alkaline solution may be, for example, filtering the steel-making slag in the alkaline solution through a filter screen, but in this embodiment, it is not particularly limited.

之後,在步驟S130中,在鹼性溶液中加入玻璃粉末並攪拌,以形成膠結溶液。玻璃粉末的來源可來自廢棄玻璃,舉例來說,玻璃粉末可從各種種類的廢棄玻璃容器、廢棄玻璃基板等中取得,但本實施例不以此為限,意即,其他非廢棄玻璃也可作為本實施例中玻璃粉末的來源。在本實施例中,玻璃粉末可由將廢棄玻璃粉碎後取得。當於鹼性溶液中加入玻璃粉末時,鹼性溶液中的氫氧根離子會與玻璃粉末進行“鹼激發反應”,以產生類似水泥漿體的膠結溶液。上述的“鹼激發反應”為藉由氫氧根離子解離玻璃粉末的矽酸鹽結構體,且玻璃粉末經解離後的物質會再重新鍵結組構。在本實施例中,玻璃粉末的比表面積為3000~20000 cm2 /g,較佳為3500~15000 cm2 /g,更佳為4000~10000 cm2 /g。玻璃粉末的比表面積在此範圍內時,由於玻璃粉末的細度足夠小,因此可提升進行“鹼激發反應”之反應速率。在本實施例中,於鹼性溶液中加入玻璃粉末的攪拌時間為10~180分,較佳為30~60分,更佳為30分。在本實施例中,於鹼性溶液中加入玻璃粉末的攪拌溫度為30°C~80°C,較佳為30°C~50°C,更佳為30°C。Thereafter, in step S130, glass powder is added to the alkaline solution and stirred to form a cementing solution. The source of glass powder can be from waste glass. For example, glass powder can be obtained from various types of waste glass containers, waste glass substrates, etc., but this embodiment is not limited to this, meaning that other non-waste glass can also be As a source of glass powder in this example. In this embodiment, the glass powder can be obtained by crushing waste glass. When glass powder is added to the alkaline solution, the hydroxide ions in the alkaline solution will undergo an "alkali excitation reaction" with the glass powder to produce a cement paste-like cementing solution. The above “alkali excitation reaction” is to dissolve the silicate structure of the glass powder by hydroxide ions, and the material after the glass powder is dissolved will be re-bonded to the structure. In this embodiment, the specific surface area of the glass powder is 3000 to 20000 cm 2 / g, preferably 3500 to 15000 cm 2 / g, and more preferably 4000 to 10000 cm 2 / g. When the specific surface area of the glass powder is within this range, since the fineness of the glass powder is sufficiently small, the reaction rate for performing the "alkali excitation reaction" can be increased. In this embodiment, the stirring time for adding the glass powder to the alkaline solution is 10 to 180 minutes, preferably 30 to 60 minutes, and more preferably 30 minutes. In this embodiment, the stirring temperature of the glass powder added to the alkaline solution is 30 ° C to 80 ° C, preferably 30 ° C to 50 ° C, and more preferably 30 ° C.

最後,在步驟S140中,固化膠結溶液,以形成膠結材。在膠結溶液經固化的過程中,膠結溶液逐漸失去可塑性而變成不具有流動性的狀態,之後膠結溶液的強度將雖著時間的推移而逐漸地增加,最後變成具有高抗壓強度的膠結材。在本實施例中,膠結溶液經固化的時間為1~14天,較佳為2~10天,更佳為5天。在本實施例中,膠結溶液經固化的溫度為40°C~95°C,較佳為60°C~90°C,更佳為80°C。膠結溶液經固化的溫度為上述溫度時可使經固化後之膠結材具有高的抗壓強度。當膠結溶液經固化的溫度小於40C時,膠結溶液經固化成膠結材的時間將會較長,甚至膠結溶液將無法固化成膠結材;當膠結溶液經固化的溫度大於95°C時,膠結溶液經固化成膠結材的時間雖然可縮短,但膠結材的抗壓強度將由於不充足的固化時間而使得其抗壓強度較低。Finally, in step S140, the cement solution is cured to form a cement material. During the curing process of the cementing solution, the cementing solution gradually loses its plasticity and becomes a state without fluidity. After that, the strength of the cementing solution will gradually increase despite the passage of time, and finally it will become a cementitious material with high compressive strength. In this embodiment, the curing time of the cementing solution is 1-14 days, preferably 2-10 days, and more preferably 5 days. In this embodiment, the curing temperature of the cementing solution is 40 ° C to 95 ° C, preferably 60 ° C to 90 ° C, and more preferably 80 ° C. When the curing temperature of the cementing solution is the above temperature, the cemented material after curing can have high compressive strength. When the curing temperature of the cement solution is less than 40C, the time for the cement solution to cure into cement material will be longer, and even the cement solution will not be cured into cement material; when the curing temperature of the cement solution is greater than 95 ° C, the cement solution Although the time of curing into a cement material can be shortened, the compressive strength of the cement material will be lower due to insufficient curing time.

另外,膠結溶液中的煉鋼爐渣與玻璃粉末的重量比例也會影響膠結溶液經固化後形成膠結材的抗壓強度,在本實施例中,煉鋼爐渣可為轉爐石或電弧爐渣,因此,於此處以膠結材中的轉爐石的含量為例。如圖4及表3所示,在膠結溶液經固化的溫度為80°C以及其固化時間為15 min的情況下,當膠結材中的轉爐石的含量的範圍為10%~70%時,膠結材可具有高的抗壓強度。由於本發明的目的為消耗大量的煉鋼爐渣,因此,膠結材中的轉爐石的含量的範圍較佳為20%~50%,更佳為接近50%。In addition, the weight ratio of the steel-making slag to the glass powder in the cementing solution will also affect the compressive strength of the cemented material after the cementing solution is cured. In this embodiment, the steel-making slag may be converter stone or electric arc slag. Therefore, Here, the content of the converter stone in the cement material is taken as an example. As shown in Fig. 4 and Table 3, when the curing temperature of the cement solution is 80 ° C and the curing time is 15 min, when the content of the converter stone in the cement material ranges from 10% to 70%, The cement material can have high compressive strength. Since the purpose of the present invention is to consume a large amount of steel-making slag, the range of the content of the converter stone in the cement material is preferably 20% to 50%, more preferably close to 50%.

表3 table 3

本實施例中的膠結材的製造方法將煉鋼爐渣及廢棄玻璃作為形成膠結材的原料之一,除可將煉鋼爐渣及廢棄玻璃回收再利用外,亦可使處理煉鋼爐渣及廢棄玻璃所需的成本與形成膠結材的原料成本降低。另外,本實施例藉由將煉鋼爐渣浸泡在水中產生氫氧根離子,以使氫氧根離子與玻璃粉末進行“鹼激發反應”,由於玻璃粉末在pH值>11的鹼性溶液下即可進行“鹼激發反應”,本實施例藉由控制煉鋼爐渣於鹼性溶液中的浸泡溫度,可確保鹼性溶液的pH值>11,因此,可不需額外購買鹼金屬或鹼土金屬之氫氧化物及矽酸鈉等來自備鹼性溶液,而使形成膠結材的原料成本降低。The method of manufacturing cemented materials in this embodiment uses steel-making slag and waste glass as one of the raw materials for forming the cement material. In addition to recycling steel-making slag and waste glass, it is also possible to process steel-making slag and waste glass. The cost required and the cost of raw materials for forming the cement material are reduced. In addition, in this embodiment, hydroxide ions are generated by immersing the steel-making slag in water, so that the hydroxide ions and the glass powder undergo an "alkali excitation reaction", because the glass powder is under an alkaline solution with a pH value of> 11. The “alkaline excitation reaction” can be carried out. In this embodiment, by controlling the immersion temperature of the steelmaking slag in the alkaline solution, the pH value of the alkaline solution can be ensured to be greater than 11. Therefore, there is no need to purchase additional hydrogen of alkali metals or alkaline earth metals Oxides and sodium silicate come from the preparation of alkaline solutions, which reduces the cost of raw materials for forming cement.

圖2為本發明的第一實施例的砂漿固化物的製造方法的步驟流程圖。FIG. 2 is a flowchart of the steps of the method for manufacturing a mortar cured product according to the first embodiment of the present invention.

請參照圖2,步驟S200、S210分別與圖1所示的步驟S100、S110相同,因此以下不再贅述。Please refer to FIG. 2. Steps S200 and S210 are the same as steps S100 and S110 shown in FIG. 1 respectively, so they are not described below.

請繼續參照圖2,在步驟S220中,於鹼性溶液中加入玻璃粉末並攪拌,以形成砂漿。當於鹼性溶液中加入玻璃粉末時,鹼性溶液中的氫氧根離子會與玻璃粉末進行“鹼激發反應”,以於鹼性溶液中產生膠結體,而膠結體之後會與鹼性溶液中的煉鋼爐渣混合以形成砂漿。玻璃粉末的來源、種類及其比表面積的範圍已記述於上述膠結材的製造方法的實例中,因此不再贅述。在本實施例中,於鹼性溶液中加入玻璃粉末的攪拌時間為5分以上,較佳為20分以上,更佳為30分以上。Please continue to refer to FIG. 2. In step S220, glass powder is added to the alkaline solution and stirred to form a mortar. When glass powder is added to the alkaline solution, the hydroxide ions in the alkaline solution will undergo an “alkali excitation reaction” with the glass powder to produce cement in the alkaline solution, and the cement will then react with the alkaline solution The steelmaking slag in the mixes to form a mortar. The source, type and range of the specific surface area of the glass powder have already been described in the above-mentioned example of the manufacturing method of the cement material, and therefore will not be repeated here. In this embodiment, the stirring time for adding the glass powder to the alkaline solution is 5 minutes or more, preferably 20 minutes or more, and more preferably 30 minutes or more.

最後,在步驟S230中,固化砂漿,以形成砂漿固化物。在砂漿經固化的過程中,砂漿逐漸失去可塑性而變成不具有流動性的狀態,之後砂漿的強度將隨著時間的推移而逐漸地增加,最後變成具有高抗壓強度的砂漿固化物。在本實施例中,砂漿經固化的時間為2~8天,較佳為4~7天,更佳為6天。在本實施例中,砂漿經固化的溫度為30°C~80°C,較佳為60°C~70°C,更佳為60°C。砂漿經固化的溫度為上述溫度時可使經固化後之砂漿固化物具有高的抗壓強度。當砂漿經固化的溫度小於30°C時,砂漿經固化成砂漿固化物的時間將會較長,甚至砂漿將無法固化成砂漿固化物;當砂漿經固化的溫度大於80°C時,砂漿經固化成砂漿固化物的時間雖然可縮短,但砂漿固化物的抗壓強度將由於不充足的固化時間而使得其抗壓強度較低。Finally, in step S230, the mortar is cured to form a cured mortar. During the curing process of the mortar, the mortar gradually loses its plasticity and becomes a state of no fluidity, after which the strength of the mortar will gradually increase with time, and finally become a mortar cured product with high compressive strength. In this embodiment, the curing time of the mortar is 2-8 days, preferably 4-7 days, and more preferably 6 days. In this embodiment, the cured temperature of the mortar is 30 ° C to 80 ° C, preferably 60 ° C to 70 ° C, and more preferably 60 ° C. When the curing temperature of the mortar is the above temperature, the cured mortar can have high compressive strength. When the curing temperature of the mortar is less than 30 ° C, the curing time of the mortar into the cured mortar will be longer, and even the mortar will not be cured into the cured mortar; when the curing temperature of the mortar is greater than 80 ° C, the mortar will Although the time for curing into a mortar cured product can be shortened, the compressive strength of the mortar cured product will be lower due to insufficient curing time.

本實施例中的砂漿固化物的製造方法由於與上述的膠結材的製造方法的實施例皆將煉鋼爐渣及廢棄玻璃作為原料,因此,可使處理煉鋼爐渣及廢棄玻璃所需的成本以及形成砂漿固化物的原料成本降低。另外,本實施例也使煉鋼爐渣浸泡在水中以產生氫氧根離子,並藉由控制煉鋼爐渣於鹼性溶液中的浸泡溫度,確保鹼性溶液的pH值>11,因此,可不需額外購買鹼金屬或鹼土金屬之氫氧化物及矽酸鈉等來自備鹼性溶液,而使形成砂漿固化物的原料成本降低。The manufacturing method of the mortar cured product in this embodiment uses steel-making slag and waste glass as raw materials in the examples of the above-mentioned cement material manufacturing method. Therefore, the cost required for processing the steel-making slag and waste glass and the The cost of raw materials forming the mortar cured product is reduced. In addition, in this embodiment, the steel-making slag is immersed in water to generate hydroxide ions, and by controlling the immersion temperature of the steel-making slag in the alkaline solution, the pH of the alkaline solution is ensured to be greater than 11. Therefore, it is not necessary The additional purchase of alkali metal or alkaline earth metal hydroxides and sodium silicate comes from the preparation of alkaline solutions, which reduces the cost of raw materials for forming mortar cured products.

圖3為本發明的第二實施例的砂漿固化物的製造方法的步驟流程圖。3 is a flowchart of steps of a method for manufacturing a mortar cured product according to a second embodiment of the invention.

請參照圖3,步驟S300、S310、S320分別與圖1所示的步驟S100、S110、S120相同,因此以下不再贅述。Referring to FIG. 3, steps S300, S310, and S320 are the same as steps S100, S110, and S120 shown in FIG. 1, respectively, so details are not described below.

請繼續參照圖3,在步驟S330中,於鹼性溶液中加入玻璃粉末及細粒料並攪拌,以形成砂漿。當於鹼性溶液中加入玻璃粉末時,鹼性溶液中的氫氧根離子會與玻璃粉末進行“鹼激發反應”,以於鹼性溶液中產生膠結體,而膠結體之後會與鹼性溶液中的細粒料混合以形成砂漿。細粒料可例如是細砂、粒徑較小的石頭等,但在本實施例中不以此為限。在本實施例中,細粒料的粒徑小於4.75 mm。而玻璃粉末的來源、種類及其比表面積的範圍已記述於上述膠結材的製造方法的實例中,因此不再贅述。在本實施例中,於鹼性溶液中加入玻璃粉末及細粒料的攪拌時間為5分以上,較佳為20分以上,更佳為30分以上。Please continue to refer to FIG. 3. In step S330, glass powder and fine particles are added to the alkaline solution and stirred to form a mortar. When glass powder is added to the alkaline solution, the hydroxide ions in the alkaline solution will undergo an “alkali excitation reaction” with the glass powder to produce cement in the alkaline solution, and the cement will then react with the alkaline solution The fine particles in the mixture are mixed to form a mortar. The fine particles may be, for example, fine sand, stones with small particle diameters, etc., but in this embodiment, it is not limited thereto. In this embodiment, the particle size of the fine particles is less than 4.75 mm. The source, type and range of the specific surface area of the glass powder have already been described in the above-mentioned example of the manufacturing method of the cement material, and therefore will not be described in detail. In this embodiment, the stirring time for adding the glass powder and the fine particles to the alkaline solution is 5 minutes or more, preferably 20 minutes or more, and more preferably 30 minutes or more.

最後,在步驟S340中,固化砂漿,以形成砂漿固化物。在本實施例中,砂漿經固化的時間為2~8天,較佳為4~7天,更佳為6天。在本實施例中,砂漿經固化的溫度為30°C~80°C,較佳為60°C~70°C,更佳為60°C。砂漿經固化的溫度為上述溫度時可使經固化後之砂漿固化物具有高的抗壓強度。當砂漿經固化的溫度小於30°C時,砂漿經固化成砂漿固化物的時間將會較長,甚至砂漿將無法固化成砂漿固化物;當砂漿經固化的溫度大於80°C時,砂漿經固化成砂漿固化物的時間雖然可縮短,但砂漿固化物的抗壓強度將由於不充足的固化時間而使得其抗壓強度較低。Finally, in step S340, the mortar is cured to form a cured mortar. In this embodiment, the curing time of the mortar is 2-8 days, preferably 4-7 days, and more preferably 6 days. In this embodiment, the cured temperature of the mortar is 30 ° C to 80 ° C, preferably 60 ° C to 70 ° C, and more preferably 60 ° C. When the curing temperature of the mortar is the above temperature, the cured mortar can have high compressive strength. When the curing temperature of the mortar is less than 30 ° C, the time for the mortar to cure into the mortar cured product will be longer, and even the mortar will not be cured into the mortar cured product; Although the time for curing into a mortar cured product can be shortened, the compressive strength of the mortar cured product will be lower due to insufficient curing time.

本實施例中的砂漿固化物的製造方法由於與上述的膠結材的製造方法的實施例皆將煉鋼爐渣及廢棄玻璃作為原料,因此,可使處理煉鋼爐渣及廢棄玻璃所需的成本以及形成砂漿固化物的原料成本降低。另外,本實施例也使煉鋼爐渣浸泡在水中以產生氫氧根離子,並藉由控制煉鋼爐渣於鹼性溶液中的浸泡溫度,確保鹼性溶液的pH值>11,因此,可不需額外購買鹼金屬或鹼土金屬之氫氧化物及矽酸鈉等來自備鹼性溶液,而使形成砂漿固化物的原料成本降低。The manufacturing method of the mortar cured product in this embodiment uses steel-making slag and waste glass as raw materials in the examples of the above-mentioned cement material manufacturing method. Therefore, the cost required for processing the steel-making slag and waste glass and the The cost of raw materials forming the mortar cured product is reduced. In addition, in this embodiment, the steel-making slag is immersed in water to generate hydroxide ions, and by controlling the immersion temperature of the steel-making slag in the alkaline solution, the pH of the alkaline solution is ensured to be greater than 11. Therefore, it is not necessary The additional purchase of alkali metal or alkaline earth metal hydroxides and sodium silicate comes from the preparation of alkaline solutions, which reduces the cost of raw materials for forming mortar cured products.

圖5為本發明的在砂漿經固化的溫度為60°C以及轉爐石與玻璃粉末(BOF/GL)的重量比例為1:1的情況下,第一實施例的砂漿固化物分別在放置於空氣中0天、7天、28天的抗壓強度與固化時間的關係曲線圖。FIG. 5 shows the cured mortar of the first embodiment placed in the case of the present invention where the cured mortar temperature is 60 ° C and the weight ratio of converter stone to glass powder (BOF / GL) is 1: 1. The graph of the relationship between the compressive strength of 0 days, 7 days and 28 days in the air and the curing time.

請參照圖5,在第一實施例的砂漿固化物的固化時間經過2天後,砂漿固化物的抗壓強度開始隨著固化時間而顯著地上升,且在砂漿固化物的固化時間經過5天後,砂漿固化物的抗壓強度無論是在放置於空氣中0天、7天或28天的情況下皆超過30 MPa。意即,僅管第一實施例的砂漿固化物中包括煉鋼爐渣,與一般土木業常用的砂漿固化物相比,其仍具有相當的抗壓強度。Referring to FIG. 5, after 2 days of curing time of the mortar cured product of the first embodiment, the compressive strength of the mortar cured product began to rise significantly with the curing time, and the curing time of the mortar cured product passed 5 days Afterwards, the compressive strength of the mortar cured product exceeded 30 MPa when placed in the air for 0 days, 7 days or 28 days. That is to say, although the mortar cured product of the first embodiment includes steel-making slag, it still has a considerable compressive strength compared to the mortar cured product commonly used in the general civil industry.

綜上所述,本發明的膠結材及砂漿固化物的製造方法將煉鋼爐渣及廢棄玻璃作為形成膠結材的原料之一,除可將煉鋼爐渣及廢棄玻璃回收再利用外,亦可使處理煉鋼爐渣及廢棄玻璃所需的成本與形成膠結材及砂漿固化物的原料成本降低。另外,本發明藉由將煉鋼爐渣浸泡在水中以形成鹼性溶液,藉由鹼性溶液中的氫氧根離子與玻璃粉末進行反應,並藉由控制煉鋼爐渣於鹼性溶液中的浸泡溫度,確保鹼性溶液的pH值>11,因此,可不需額外購買鹼金屬或鹼土金屬之氫氧化物及矽酸鈉等來自備鹼性溶液,而使形成膠結材及砂漿固化物的原料成本降低。In summary, the manufacturing method of the cement material and the mortar cured product of the present invention uses steel-making slag and waste glass as one of the raw materials for forming the cement material. In addition to recycling the steel-making slag and waste glass, it can also be used The cost of processing steel-making slag and waste glass and the cost of raw materials for forming cement and mortar solidification are reduced. In addition, the present invention forms an alkaline solution by soaking the steelmaking slag in water, reacts with the hydroxide ions in the alkaline solution and the glass powder, and controls the immersion of the steelmaking slag in the alkaline solution The temperature ensures that the pH of the alkaline solution is greater than 11. Therefore, it is not necessary to purchase additional alkali metal or alkaline earth metal hydroxides and sodium silicate, etc. from the preparation of the alkaline solution, so that the raw material cost of forming the cement and mortar cured material reduce.

雖然本發明已以實施例揭露如上,然其並非用以限定本發明,任何所屬技術領域中具有通常知識者,在不脫離本發明的精神和範圍內,當可作些許的更動與潤飾,故本發明的保護範圍當視後附的申請專利範圍所界定者為準。Although the present invention has been disclosed as above with examples, it is not intended to limit the present invention. Any person with ordinary knowledge in the technical field can make some changes and modifications without departing from the spirit and scope of the present invention. The scope of protection of the present invention shall be subject to the scope defined in the appended patent application.

S100、S110、S120、S130、S140、S200、S210、S220、S230、S300、S310、S320、S330、S340‧‧‧步驟 S100, S110, S120, S130, S140, S200, S210, S220, S230, S300, S310, S320, S330, S340

圖1為本發明的一實施例的膠結材的製造方法的步驟流程圖。 圖2為本發明的第一實施例的砂漿固化物的製造方法的步驟流程圖。 圖3為本發明的第二實施例的砂漿固化物的製造方法的步驟流程圖。 圖4為本發明的在膠結溶液經攪拌的溫度為80°C以及其攪拌時間為15 min的情況下,膠結材中的轉爐石的含量以及膠結材的抗壓強度的關係曲線圖。 圖5為本發明的在砂漿經固化的溫度為60°C以及轉爐石與玻璃粉末(BOF/GL)的重量比例為1:1的情況下,第一實施例的砂漿固化物分別在放置於空氣中0天、7天、28天的抗壓強度與固化時間的關係曲線圖。FIG. 1 is a flowchart of steps of a method for manufacturing a cement material according to an embodiment of the invention. FIG. 2 is a flowchart of the steps of the method for manufacturing a mortar cured product according to the first embodiment of the present invention. 3 is a flowchart of steps of a method for manufacturing a mortar cured product according to a second embodiment of the invention. 4 is a graph showing the relationship between the content of the converter stone in the cement material and the compressive strength of the cement material when the temperature of the cement solution is 80 ° C. and the stirring time is 15 min. FIG. 5 shows the cured mortar of the first embodiment placed in the case of the present invention where the cured mortar temperature is 60 ° C and the weight ratio of converter stone to glass powder (BOF / GL) is 1: 1. The graph of the relationship between the compressive strength of 0 days, 7 days and 28 days in the air and the curing time.

S100、S110、S120、S130、S140、S200、S210、S220、S230、S300、S310、S320、S330、S340‧‧‧步驟 S100, S110, S120, S130, S140, S200, S210, S220, S230, S300, S310, S320, S330, S340

Claims (20)

一種膠結材的製造方法,其包括下列步驟: 提供煉鋼爐渣; 將所述煉鋼爐渣浸泡在水中,以使水形成鹼性溶液; 將所述鹼性溶液與所述煉鋼爐渣分離; 在所述鹼性溶液中加入玻璃粉末並攪拌,以形成膠結溶液;以及 固化所述膠結溶液,以形成膠結材。A method for manufacturing a cement material, comprising the following steps: providing a steel-making slag; soaking the steel-making slag in water to form an alkaline solution in the water; separating the alkaline solution from the steel-making slag; Glass powder is added to the alkaline solution and stirred to form a cementing solution; and the cementing solution is cured to form a cementing material. 如申請專利範圍第1項所述的膠結材的製造方法,其中所述煉鋼爐渣包括轉爐石或電弧爐渣。The method for manufacturing a cement material as described in item 1 of the patent application scope, wherein the steel-making slag includes converter stone or electric arc slag. 如申請專利範圍第2項所述的膠結材的製造方法,其中在將所述煉鋼爐渣浸泡在水的步驟中,水(W)與所述轉爐石(BOF)的重量比例(W/BOF)為0.25~2.0。The method for manufacturing a cement material as described in item 2 of the patent application scope, wherein in the step of immersing the steel-making slag in water, the weight ratio of water (W) to the converter stone (BOF) (W / BOF ) Is 0.25 ~ 2.0. 如申請專利範圍第1項所述的膠結材的製造方法,其中所述玻璃粉末的比表面積為3000~20000 cm2 /g。The method for manufacturing a cement material as described in item 1 of the patent application range, wherein the specific surface area of the glass powder is 3,000 to 20,000 cm 2 / g. 如申請專利範圍第1項所述的膠結材的製造方法,其中在將所述煉鋼爐渣浸泡在水的步驟中,將所述鹼性溶液的溫度調整至0°C~90°C,且在固化所述膠結溶液的步驟中,將所述膠結溶液的溫度調整至40°C~95°C。The method for manufacturing a cement material as described in item 1 of the patent application scope, wherein in the step of immersing the steel-making slag in water, the temperature of the alkaline solution is adjusted to 0 ° C to 90 ° C, and In the step of curing the cementing solution, the temperature of the cementing solution is adjusted to 40 ° C to 95 ° C. 一種砂漿固化物的製造方法,其包括下列步驟: 提供煉鋼爐渣; 將所述煉鋼爐渣浸泡在水中,以使水形成鹼性溶液; 於含所述煉鋼爐渣的所述鹼性溶液中加入玻璃粉末並攪拌,以形成砂漿;以及 固化所述砂漿,以形成砂漿固化物。A method for manufacturing a solidified mortar, comprising the following steps: providing a steel-making slag; soaking the steel-making slag in water to form an alkaline solution in the water; in the alkaline solution containing the steel-making slag Glass powder is added and stirred to form a mortar; and the mortar is cured to form a cured mortar. 如申請專利範圍第6項所述的砂漿固化物的製造方法,其中所述煉鋼爐渣包括轉爐石或電弧爐渣。The method for manufacturing a solidified mortar according to item 6 of the patent application scope, wherein the steel-making slag includes converter stone or electric arc slag. 如申請專利範圍第7項所述的砂漿固化物的製造方法,其中在將所述煉鋼爐渣浸泡在水的步驟中,水(W)與所述轉爐石(BOF)的重量比例(W/BOF)為0.25~2.0。The method for manufacturing a cured mortar according to item 7 of the patent application scope, wherein in the step of immersing the steel-making slag in water, the weight ratio of water (W) to the converter stone (BOF) (W / BOF) is 0.25 ~ 2.0. 如申請專利範圍第7項所述的砂漿固化物的製造方法,其中在於所述鹼性溶液中加入所述玻璃粉末並攪拌的步驟中,所述轉爐石(BOF)與所述玻璃粉末(GL)的重量比例(BOF/GL)為0.1~1.0。The method for manufacturing a cured mortar according to item 7 of the patent application scope, wherein in the step of adding the glass powder to the alkaline solution and stirring, the converter stone (BOF) and the glass powder (GL ) Weight ratio (BOF / GL) is 0.1 ~ 1.0. 如申請專利範圍第6項所述的砂漿固化物的製造方法,其中所述玻璃粉末的比表面積為3000~20000 cm2 /g。The method for manufacturing a cured mortar as described in item 6 of the patent application range, wherein the specific surface area of the glass powder is 3,000 to 20,000 cm 2 / g. 如申請專利範圍第6項所述的砂漿固化物的製造方法,其中在將所述煉鋼爐渣浸泡在水的步驟中,將所述鹼性溶液的溫度調整至0°C~90°C,且在固化所述砂漿的步驟中,將所述砂漿的溫度調整至30°C~80°C。The method for manufacturing a cured mortar according to item 6 of the patent application scope, wherein in the step of immersing the steel-making slag in water, the temperature of the alkaline solution is adjusted to 0 ° C to 90 ° C, And in the step of curing the mortar, the temperature of the mortar is adjusted to 30 ° C to 80 ° C. 一種砂漿固化物的製造方法,其包括下列步驟: 提供煉鋼爐渣; 將所述煉鋼爐渣浸泡在水中,以使水形成鹼性溶液; 將所述鹼性溶液與所述煉鋼爐渣分離; 於所述鹼性溶液中加入玻璃粉末及細粒料並攪拌,以形成砂漿;以及 固化所述砂漿,以形成砂漿固化物。A method for manufacturing a solidified mortar, comprising the following steps: providing steel-making slag; soaking the steel-making slag in water to form an alkaline solution in water; separating the alkaline solution from the steel-making slag; Adding glass powder and fine particles to the alkaline solution and stirring to form a mortar; and curing the mortar to form a cured mortar. 如申請專利範圍第12項所述的砂漿固化物的製造方法,其中所述煉鋼爐渣包括轉爐石或電弧爐渣。The method for manufacturing a solidified mortar according to item 12 of the patent application scope, wherein the steel-making slag includes converter stone or electric arc slag. 如申請專利範圍第13項所述的砂漿固化物的製造方法,其中在將所述煉鋼爐渣浸泡在水的步驟中,水(W)與所述轉爐石(BOF)的重量比例(W/BOF)為0.25~2.0。The method for manufacturing a cured mortar according to item 13 of the patent application scope, wherein in the step of immersing the steel-making slag in water, the weight ratio of water (W) to the converter stone (BOF) (W / BOF) is 0.25 ~ 2.0. 如申請專利範圍第12項所述的砂漿固化物的製造方法,其中所述玻璃粉末的比表面積為3000~20000 cm2 /g。The method for manufacturing a cured mortar as described in item 12 of the patent application range, wherein the specific surface area of the glass powder is 3,000 to 20,000 cm 2 / g. 如申請專利範圍第12項所述的砂漿固化物的製造方法,其中在將所述煉鋼爐渣浸泡在水的步驟中,將所述鹼性溶液的溫度調整至0°C~90°C,且在固化所述砂漿的步驟中,將所述砂漿的溫度調整至30°C~80°C。The method for manufacturing a cured mortar according to item 12 of the patent application scope, wherein in the step of immersing the steel-making slag in water, the temperature of the alkaline solution is adjusted to 0 ° C to 90 ° C, And in the step of curing the mortar, the temperature of the mortar is adjusted to 30 ° C to 80 ° C. 一種砂漿固化物,其包括: 10~50 wt%的煉鋼爐渣;以及 50~90 wt%的如申請專利範圍第1項所述的膠結材。A solidified mortar, comprising: 10-50 wt% of steel-making slag; and 50-90 wt% of cementitious material as described in item 1 of the patent application scope. 如申請專利範圍第17項所述的砂漿固化物,其中所述煉鋼爐渣包括轉爐石或電弧爐渣。The solidified mortar according to item 17 of the patent application scope, wherein the steel-making slag includes converter stone or electric arc slag. 如申請專利範圍第17項所述的砂漿固化物,其中所述煉鋼爐渣的粒徑小於4.75 mm。The mortar cured product as described in Item 17 of the patent application scope, wherein the particle size of the steel-making slag is less than 4.75 mm. 如申請專利範圍第17項所述的砂漿固化物,其中所述玻璃粉末的比表面積為3000~20000 cm2 /g。The mortar cured product as described in item 17 of the patent application range, wherein the specific surface area of the glass powder is 3,000 to 20,000 cm 2 / g.
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