TWI873655B - Method for manufacturing floor bricks using solid recovered fuel fly ash and bottom ash - Google Patents
Method for manufacturing floor bricks using solid recovered fuel fly ash and bottom ash Download PDFInfo
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract
Description
本發明係關於一種方法,特別是一種應用混燒灰渣製備地磚之方法。 The present invention relates to a method, in particular a method for preparing floor tiles using mixed-burning ash.
由於經濟快速發展除了造成自然資源的過度開採外,廢棄物的產出也與日俱增,特別是紡織業、光電面板業、半導體產業及造紙業...等企業於生產製程所衍生之廢棄物以及所衍生之有害事業廢棄物。 In addition to the over-exploitation of natural resources, the rapid economic development has also led to an increase in waste generation, especially waste generated by the production processes of the textile, photovoltaic panel, semiconductor and paper industries, as well as hazardous industrial waste.
針對上述廢棄物,目前政府除了積極推動由產業的源頭進行減量外,亦致力於將上述廢棄物進行回收後再利用。 Regarding the above waste, the government is currently actively promoting reduction at the source of the industry and is also committed to recycling and reusing the above waste.
為此,對於回收廢棄物再進行利用的想法,近年來環保署極力推廣「固體再生燃料」(Solid Recovered Fuel,簡稱SRF)的使用,其固體再生燃料亦可稱為固體回收燃料或固體再利用燃料。 To this end, in recent years, the Environmental Protection Agency has been vigorously promoting the use of "Solid Recovered Fuel" (SRF) to recycle waste. Solid recovered fuel can also be called solid recovered fuel or solid reused fuel.
固體再生燃料(SRF)由塑料與生質物(如廢紙、木材與其他木質纖維廢棄物)等非有害且具適燃性物質以及符合燃料品質標準(分別為淨熱值、氯含量、汞含量、鉛含量以及鎘含量)的回收所轉製而成。固體再生燃料(SRF)具 有低環境衝擊、低燃料成本、並可應用於高能源效率鍋爐及燃燒設施等三大優勢。 Solid renewable fuel (SRF) is converted from non-hazardous and flammable materials such as plastics and biomass (such as waste paper, wood and other wood fiber waste) and meets fuel quality standards (net calorific value, chlorine content, mercury content, lead content and cadmium content). Solid renewable fuel (SRF) has three major advantages: low environmental impact, low fuel cost, and can be used in high-energy-efficiency boilers and combustion facilities.
固體再生燃料(SRF)相較於煤炭,固體再生燃料(SRF)作為燃料更能達成減碳之效。此外,將適燃性廢棄物分離製成固體再生燃料(SRF)做為工業鍋爐燃料使用,也可減少現有焚化爐負荷。 Solid renewable fuel (SRF) is more effective in reducing carbon emissions than coal. In addition, separating combustible waste into solid renewable fuel (SRF) for use as industrial boiler fuel can also reduce the load on existing incinerators.
目前,現有的固體再生燃料(SRF)主要之使用者為工業用鍋爐、水泥旋窯、煉鋼業熔爐及煉焦爐、專用燃燒發電設備等等,不涵蓋廢棄物焚化裝置。 At present, the main users of existing solid renewable fuel (SRF) are industrial boilers, cement kilns, steelmaking furnaces and coke furnaces, special combustion power generation equipment, etc., and do not cover waste incineration equipment.
而根據環保署所制訂的「固體再生燃料製造技術指引與品質規範」符合固體再生燃料(SRF)的廢棄物種類有廢塑膠(廢PET、廢PP、廢PE及廢PLA等等)、廢橡膠、廢紙、廢木材、廢纖維(廢布、廢人造纖維及紡織殘料等)、汙泥、動植物性廢棄物(蔗渣)及垃圾等等。 According to the "Technical Guidelines and Quality Specifications for the Production of Solid Renewable Fuels" formulated by the Environmental Protection Administration, the types of waste that meet the requirements for solid renewable fuels (SRF) include waste plastics (waste PET, waste PP, waste PE and waste PLA, etc.), waste rubber, waste paper, waste wood, waste fiber (waste cloth, waste man-made fiber and textile residues, etc.), sludge, animal and plant waste (bagasse) and garbage, etc.
然而,在循環式流體化床鍋爐中燃燒固體再生燃料(SRF),仍會產生混燒灰及混燒底渣,且由於混燒灰及混燒底渣的成分多元、複雜,仍會造成對環境造成不小的負擔。 However, burning solid renewable fuel (SRF) in a circulating fluidized bed boiler will still produce mixed combustion ash and mixed combustion bottom ash, and because the components of mixed combustion ash and mixed combustion bottom ash are diverse and complex, they will still cause a considerable burden on the environment.
而於現今環保意識下,將燃燒固體再生燃料(SRF)後產生的混燒灰及混燒底渣再此進行利用是非常必要且須被大力推廣的。 With today's environmental awareness, it is very necessary to reuse the mixed combustion ash and mixed combustion bottom ash produced after burning solid renewable fuel (SRF) and it must be vigorously promoted.
為此,如何將燃燒固體再生燃料(SRF)後產生的混燒灰及混燒底渣再此回收進行利用,為本領域技術人員所欲解決的問題。 Therefore, how to recycle the mixed combustion ash and mixed combustion bottom ash produced after burning solid renewable fuel (SRF) for reuse is a problem that technicians in this field want to solve.
本發明之一目的,在於提供一種應用混燒灰渣製備地磚之方法,使用爐石粉作為無機聚合技術之原料,搭配天然砂及鹼性溶液並以混燒灰及混燒底渣取代天然砂後進行混拌,透過高壓製成磚體,有效將混燒灰及混燒底渣進行資源化運用,更可以於產品製作過程減少使用水泥粉所產生之二氧化碳。 One of the purposes of the present invention is to provide a method for preparing floor tiles using calcined ash, using furnace stone powder as the raw material of inorganic polymerization technology, mixing with natural sand and alkaline solution, and replacing natural sand with calcined ash and calcined bottom ash, and making brick bodies through high pressure, effectively utilizing calcined ash and calcined bottom ash as resources, and reducing the carbon dioxide generated by the use of cement powder in the product manufacturing process.
針對上述之目的,本發明提供一種應用混燒灰渣製備地磚之方法,其包含:取一固體再生燃料進行一燃燒製程後,產生一混燒灰以及一混燒底渣;取該混燒灰及一爐石粉進行混拌,並依據一攪拌比例加入一天然砂或/及該混燒底渣混拌一第一時間後,形成一混合底料;取該混合底料與一鹼性溶液依據一液固比混拌一第二時間後,形成一漿料;以及將該漿料灌入一製磚模具,並依據一壓力進行一高壓製程後,形成一地磚。 To achieve the above-mentioned purpose, the present invention provides a method for preparing floor tiles using mixed ash, which comprises: taking a solid renewable fuel and performing a combustion process to generate a mixed ash and a mixed bottom ash; taking the mixed ash and a furnace stone powder for mixing, and adding a natural sand and/or the mixed bottom ash according to a mixing ratio for a first time to form a mixed bottom material; taking the mixed bottom material and an alkaline solution and mixing them according to a liquid-solid ratio for a second time to form a slurry; and pouring the slurry into a brick-making mold, and performing a high-pressure process according to a pressure to form a floor tile.
本發明提供一實施例,其中於取該混燒灰及一爐石粉進行混拌,並依據一攪拌比例加入一天然砂或/及該混燒底渣混拌一第一時間後,形成一混合底料之步驟中,該混燒灰之一重量百分比係為20Wt%到60Wt%,該爐石粉之一重量百分比係為20Wt%。 The present invention provides an embodiment, wherein in the step of taking the calcined ash and a furnace stone powder for mixing, and adding a natural sand or/and the calcined bottom ash according to a mixing ratio and mixing for a first time to form a mixed bottom material, a weight percentage of the calcined ash is 20wt% to 60wt%, and a weight percentage of the furnace stone powder is 20wt%.
本發明提供一實施例,其中於取該混燒灰及一爐石粉進行混拌,並依據一攪拌比例加入一天然砂或/及該混燒底渣混拌一第一時間後,形成一混合底料之步驟中,該攪拌比例之該混燒底渣之一重量百分比係為0Wt%,該天然砂之一重量百分比係為20Wt%到60Wt%,進一步,該混燒灰及該天然砂之該重量百分比之總和為80Wt%。 The present invention provides an embodiment, wherein in the step of mixing the calcined ash and furnace stone powder, adding natural sand or/and the calcined bottom ash according to a mixing ratio and mixing for a first time to form a mixed bottom material, a weight percentage of the calcined bottom ash in the mixing ratio is 0wt%, a weight percentage of the natural sand is 20wt% to 60wt%, and further, the sum of the weight percentages of the calcined ash and the natural sand is 80wt%.
本發明提供一實施例,其中於取該混燒灰及一爐石粉進行混拌,並依據一攪拌比例加入一天然砂或/及該混燒底渣混拌一第一時間後,形成 一混合底料之步驟中,該攪拌比例之該混燒底渣之一重量百分比係為40Wt%到60Wt%,該天然砂之一重量百分比係為0Wt%,進一步,該混燒灰及該混燒底渣之該重量百分比之總和為80Wt%。 The present invention provides an embodiment, wherein in the step of forming a mixed base material by mixing the calcined ash and a furnace stone powder, and adding a natural sand or/and the calcined bottom ash according to a mixing ratio and mixing for a first time, a weight percentage of the calcined bottom ash in the mixing ratio is 40wt% to 60wt%, a weight percentage of the natural sand is 0wt%, and further, the sum of the weight percentages of the calcined ash and the calcined bottom ash is 80wt%.
本發明提供一實施例,其中於取該混燒灰及一爐石粉進行混拌,並依據一攪拌比例加入一天然砂或/及該混燒底渣混拌一第一時間後,形成一混合底料之步驟中,該攪拌比例之該混燒底渣之一重量百分比係為10Wt%,該天然砂之一重量百分比係為10Wt%。 The present invention provides an embodiment, wherein in the step of taking the mixed ash and a furnace stone powder for mixing, and adding a natural sand or/and the mixed bottom ash for mixing for a first time according to a mixing ratio to form a mixed bottom material, the mixing ratio has a weight percentage of the mixed bottom ash of 10wt% and a weight percentage of the natural sand of 10wt%.
本發明提供一實施例,其中於取該混合底料與一鹼性溶液依據一液固比混拌一第二時間後,形成一漿料後之步驟中,該鹼性溶液係為一鈉鹽溶液。 The present invention provides an embodiment, wherein in the step of taking the mixed base material and an alkaline solution and mixing them for a second time according to a liquid-to-solid ratio to form a slurry, the alkaline solution is a sodium salt solution.
本發明提供一實施例,其中該鈉鹽溶液係為一NaOH溶液或一Na2SO3溶液。 The present invention provides an embodiment, wherein the sodium salt solution is a NaOH solution or a Na 2 SO 3 solution.
本發明提供一實施例,其中於取該混合底料與一鹼性溶液依據一液固比混拌一第二時間後,形成一漿料後之步驟中,該液固比係介於0.2至0.3之間。 The present invention provides an embodiment, wherein in the step of taking the mixed base material and an alkaline solution and mixing them for a second time according to a liquid-to-solid ratio to form a slurry, the liquid-to-solid ratio is between 0.2 and 0.3.
本發明提供一實施例,其中於將該漿料灌入一製磚模具,並依據一壓力進行一高壓製程後,形成一地磚之步驟中,該壓力係介於70Kgf/cm2至90Kgf/cm2之間。 The present invention provides an embodiment, wherein in the step of forming a floor tile after pouring the slurry into a tile-making mold and performing a high-pressure process according to a pressure, the pressure is between 70Kgf/ cm2 and 90Kgf/ cm2 .
S10:步驟 S10: Step
S20:步驟 S20: Step
S30:步驟 S30: Step
S40:步驟 S40: Step
第1圖:其為本發明之一實施例之應用混燒灰渣製備地磚之方法之流程示意圖。 Figure 1: It is a schematic diagram of the process of preparing floor tiles using mixed burning ash in one embodiment of the present invention.
為使 貴審查委員對本發明之特徵及所達成之功效有更進一步之瞭解與認識,謹佐以較佳之實施例及配合詳細之說明,說明如後:習知由固體再生燃料中產生的混燒灰及混燒底渣,是由新型固體再生燃料(SRF)放入循環式流體化床鍋爐燃燒後所產生之產物,由於混燒灰及混燒底渣會造成過度膨脹,而導致強度下降,再者也因為混燒灰及混燒底渣之組成成分複雜,因此會對環境造成負擔。 In order to enable the review committee to have a deeper understanding and recognition of the characteristics and effects of the present invention, the preferred embodiments and detailed descriptions are provided as follows: It is known that the mixed combustion ash and mixed combustion bottom ash produced from solid renewable fuel are products produced after the new solid renewable fuel (SRF) is put into a circulating fluidized bed boiler for combustion. Since the mixed combustion ash and mixed combustion bottom ash will cause excessive expansion, resulting in a decrease in strength, and because the composition of the mixed combustion ash and mixed combustion bottom ash is complex, it will cause a burden on the environment.
本發明改良了一種應用混燒灰渣製備地磚之方法,使用爐石粉作為無機聚合技術之原料,搭配天然砂及鹼性溶液並以混燒灰及混燒底渣取代天然砂後進行混拌,透過高壓製成磚體,有效將混燒灰及混燒底渣進行資源化運用,更可以於產品製作過程減少使用水泥粉所產生之二氧化碳。 The present invention improves a method for preparing floor tiles using mixed ash and slag, using furnace stone powder as the raw material of inorganic polymerization technology, mixing with natural sand and alkaline solution, and replacing natural sand with mixed ash and mixed bottom slag, and making brick bodies through high pressure, effectively utilizing mixed ash and mixed bottom slag as resources, and reducing the carbon dioxide generated by the use of cement powder in the product manufacturing process.
在下文中,將藉由圖式來說明本發明之各種實施例來詳細描述本發明。然而本發明之概念可能以許多不同型式來體現,且不應解釋為限於本文中所闡述之例示性實施例。 In the following, the present invention will be described in detail by illustrating various embodiments of the present invention with reference to drawings. However, the concept of the present invention may be embodied in many different forms and should not be construed as being limited to the exemplary embodiments described herein.
首先,請參閱第1圖,其為本發明之一實施例之應用混燒灰渣製備地磚之方法之流程示意圖,如圖所示,其步驟包含:步驟S10:取固體再生燃料進行燃燒製程後,產生混燒灰以及混燒底渣; 步驟S20:取混燒灰及爐石粉進行混拌,並依據攪拌比例加入天然砂或/及混燒底渣混拌第一時間後,形成混合底料;步驟S30:取混合底料與鹼性溶液依據液固比混拌第二時間後,形成漿料;以及步驟S40:將漿料灌入製磚模具,並依據壓力進行高壓製程後,形成地磚。 First, please refer to Figure 1, which is a schematic diagram of the process of using mixed ash to prepare floor tiles according to an embodiment of the present invention. As shown in the figure, the steps include: Step S10: After taking solid renewable fuel for combustion process, mixed ash and mixed bottom ash are generated; Step S20: Mixing the mixed ash and furnace stone powder, and adding natural sand and/or mixed bottom ash according to the mixing ratio for a first time to form a mixed base material; Step S30: Mixing the mixed base material and alkaline solution according to the liquid-solid ratio for a second time to form a slurry; and Step S40: Pour the slurry into a brick-making mold, and perform a high-pressure process according to the pressure to form a floor tile.
於本實施例中,如步驟S10所述之,取一固體再生燃料進行一燃燒製程,透過該燃燒製程的過程,取得其所產生的一混燒灰以及一混燒底渣。 In this embodiment, as described in step S10, a solid renewable fuel is used to perform a combustion process, and a mixed combustion ash and a mixed combustion bottom ash are obtained through the combustion process.
其中,上述之該固體再生燃料係為以具適燃性之廢棄物,並須符合燃料品質標準,稱為SRF(Solid recovered fuel,簡稱SRF),亦可稱為固體回收燃料、固體再利用燃料或固體再生燃料。 The solid recycled fuel mentioned above is a flammable waste that must meet the fuel quality standards. It is called SRF (Solid recovered fuel, abbreviated as SRF), and can also be called solid recovered fuel, solid reused fuel or solid recycled fuel.
本實施例中之該固體再生燃料之廢棄物涵蓋非有害適燃性之事業廢棄物與一般垃圾或是事業員工垃圾兩類,其中事業廢棄物包含廢塑膠、廢橡膠、廢紙、廢木材、廢纖維、有機污泥、漿紙污泥、紡織污泥等,一般垃圾或是事業員工垃圾則通常需經由機械分選處理程序(Mechanical Treatment,MT)或機械生物處理程序(Mechanical Biological Treatment,MBT)分選後之適燃性廢棄物,方可作為該固體再生燃料之原料。 The solid renewable fuel waste in this embodiment includes non-hazardous and flammable industrial waste and general garbage or industrial employee waste. Industrial waste includes waste plastic, waste rubber, waste paper, waste wood, waste fiber, organic sludge, pulp and paper sludge, textile sludge, etc. General garbage or industrial employee waste usually needs to be separated by mechanical sorting (MT) or mechanical biological treatment (MBT) to be used as the raw material of the solid renewable fuel.
於本實施例中,該燃燒製程係使用循環是鍋爐、工業用鍋爐、水泥旋窯、煉鋼業熔爐、煉焦爐或專用燃燒發電設備之其中之一,本實施例係使用循環式鍋爐作為說明,但不僅限於此。 In this embodiment, the combustion process uses a circulating boiler, an industrial boiler, a cement kiln, a steelmaking furnace, a coke furnace, or a dedicated combustion power generation equipment. This embodiment uses a circulating boiler for illustration, but is not limited to this.
接續上述,於本實施例中,如步驟S20所述之,取得該混燒灰及該混燒底渣後,取該混燒灰及一爐石粉進行混拌,並依據一攪拌比例加入一天然砂或/及該混燒底渣混拌一第一時間後,形成一混合底料。 Continuing from the above, in this embodiment, as described in step S20, after obtaining the mixed ash and the mixed ash bottom ash, the mixed ash and a furnace stone powder are mixed, and a natural sand or/and the mixed ash bottom ash are added according to a mixing ratio and mixed for a first time to form a mixed base material.
其中,於本實施例中,該混燒灰之一重量百分比係為20Wt%到60Wt%,該爐石粉之一重量百分比係為20Wt%。 Among them, in this embodiment, the weight percentage of the mixed ash is 20Wt% to 60Wt%, and the weight percentage of the furnace stone powder is 20Wt%.
另外,於本實施例中,其中該攪拌比例之該混燒底渣係可為0Wt%,也就是說,當該攪拌比例之該混燒底渣之一重量百分比係為0Wt%,該天然砂之一重量百分比係為20Wt%到60Wt%,進一步,該混燒灰及該天然砂之該重量百分比之總和為80Wt%。 In addition, in this embodiment, the mixing ratio of the mixed ash can be 0Wt%, that is, when the mixing ratio of the mixed ash has a weight percentage of 0Wt%, the weight percentage of the natural sand is 20Wt% to 60Wt%, and further, the sum of the weight percentages of the mixed ash and the natural sand is 80Wt%.
進一步,於本實施例之中,其中該攪拌比例之該天然砂係可為0Wt%,也就是說,當該攪拌比例之該混燒底渣之一重量百分比係為40Wt%到60Wt%,該天然砂之一重量百分比係為0Wt%,進一步,該混燒灰及該混燒底渣之該重量百分比之總和為80Wt%。 Furthermore, in this embodiment, the natural sand in the mixing ratio can be 0 wt%, that is, when the weight percentage of the mixed combustion bottom ash in the mixing ratio is 40 wt% to 60 wt%, the weight percentage of the natural sand is 0 wt%, and further, the sum of the weight percentages of the mixed combustion ash and the mixed combustion bottom ash is 80 wt%.
其中,於本實施例中,係有另一較佳實施態樣,亦可以該混燒灰、該爐石粉、該天然砂以及該混燒底渣混拌,其配方組成為該混燒灰之一重量百分比係為60Wt%,該混燒底渣之一重量百分比係為10Wt%,該天然砂之一重量百分比係為10Wt%,該爐石粉之一重量百分比係為20Wt% Among them, in this embodiment, there is another preferred implementation mode, and the mixed ash, the furnace stone powder, the natural sand and the mixed ash can also be mixed, and the formula composition is that the mixed ash has a weight percentage of 60Wt%, the mixed ash has a weight percentage of 10Wt%, the natural sand has a weight percentage of 10Wt%, and the furnace stone powder has a weight percentage of 20Wt%
接續上述,請復參閱第1圖,如本實施例之步驟S30至步驟S40所述之步驟,取該混合底料與一鹼性溶液依據一液固比混拌一第二時間後,形成一漿料後,將該漿料灌入一製磚模具,並依據一壓力進行一高壓製程後,形成一地磚。 Continuing with the above, please refer to Figure 1 again. As described in steps S30 to S40 of this embodiment, the mixed base material and an alkaline solution are mixed for a second time according to a liquid-solid ratio to form a slurry, and the slurry is poured into a brick-making mold, and a high-pressure process is performed according to a pressure to form a floor tile.
其中該鹼性溶液係為一鈉鹽溶液,該鈉鹽溶液該鈉鹽溶液係為一NaOH溶液或一Na2SO3溶液。 The alkaline solution is a sodium salt solution, and the sodium salt solution is a NaOH solution or a Na 2 SO 3 solution.
於本實施例中,使用該鈉鹽溶液係由於該鈉鹼溶液係為一種習知常用的無機聚合之技術,此種技術係透過無機聚合物為一種非晶質或半晶質的材料,此材料主要以鋁矽酸鹽(Alumino-Silicate)礦物或廢棄物,置於鹼性溶液中,使Si、Al膠體由礦物表面析出,形成無機聚合物之前導物(Geopolymer Precursor)。 In this embodiment, the sodium salt solution is used because the sodium alkali solution is a commonly known inorganic polymerization technology. This technology uses an inorganic polymer as an amorphous or semi-crystalline material. This material is mainly aluminosilicate (Alumino-Silicate) minerals or wastes, which are placed in an alkaline solution to precipitate Si and Al colloids from the mineral surface to form an inorganic polymer precursor (Geopolymer Precursor).
隨後添加鹼金屬矽酸鹽溶液以提供足夠之Si離子及觸發聚合反應,形成無機聚合物的主幹,一般來說,無機聚合物的形成包括下列四個過程:(1)鋁矽酸鹽礦物粉體在鹼性溶液中的溶解;(2)溶解的矽、鋁離子由固體顆粒表面向顆粒間隙擴散;(3)鹼金屬矽酸鹽溶液和矽、鋁離子之間發生聚合反應;(4)凝膠相逐漸排除剩餘的水分,固結硬化成矽鋁無機聚合材料。 Subsequently, an alkaline metal silicate solution is added to provide sufficient Si ions and trigger a polymerization reaction to form the backbone of the inorganic polymer. Generally speaking, the formation of the inorganic polymer includes the following four processes: (1) the dissolution of aluminum silicate mineral powder in the alkaline solution; (2) the diffusion of dissolved silicon and aluminum ions from the surface of the solid particles to the gaps between the particles; (3) a polymerization reaction occurs between the alkaline metal silicate solution and the silicon and aluminum ions; (4) the gel phase gradually eliminates the remaining water and solidifies and hardens into a silicon-aluminum inorganic polymer material.
無機聚合物是由SiO4及AlO4四面體共用氧原子相互鍵結形成Si-O-Al之封閉的架狀結構,與沸石相似。其硬化機制與水泥類似為系統膠體之粒子與粒子間產生無機聚合作用。在室溫下硬化時間約為1.5-2小時,而四小時後即有80%以上之抗壓強度。其與水泥最大不同是水泥硬化後鍵結形式為水合鍵結,無機聚合物則是化學鍵結。 Inorganic polymers are formed by SiO 4 and AlO 4 tetrahedrons sharing oxygen atoms to form a closed framework structure of Si-O-Al, similar to zeolite. Its hardening mechanism is similar to that of cement, where inorganic polymerization occurs between particles of the system colloid. The hardening time at room temperature is about 1.5-2 hours, and after four hours, the compressive strength is more than 80%. The biggest difference between it and cement is that the bonding form of cement after hardening is hydration bonding, while that of inorganic polymers is chemical bonding.
透過上述之無機聚合技術,以該混合底料與一鹼性溶液依據該液固比混拌該第二時間後,形成該漿料,其中該液固比係介於0.2至0.3之間。 Through the above-mentioned inorganic polymerization technology, the mixed base material and an alkaline solution are mixed for the second time according to the liquid-solid ratio to form the slurry, wherein the liquid-solid ratio is between 0.2 and 0.3.
最後再將該漿料灌入該製磚模具中,施以該壓力使其形成本實施例所製作出之該地磚,其中,該壓力係介於70Kgf/cm2至90Kgf/cm2之間。 Finally, the slurry is poured into the brick-making mold and pressure is applied to form the floor tile made in this embodiment, wherein the pressure is between 70Kgf/ cm2 and 90Kgf/ cm2 .
本實施例之優點在於,搭配天然砂及鹼性溶液並以混燒灰及混燒底渣取代天然砂後進行混拌,透過高壓製成磚體,有效將混燒灰及混燒底渣進行資源化運用,更可以於產品製作過程減少使用水泥粉所產生之二氧化碳,讓混燒灰及混燒底渣能夠被充份利用,達到資源永續發展的目的。 The advantage of this embodiment is that natural sand and alkaline solution are used to replace natural sand with calcined ash and calcined bottom ash before mixing, and bricks are made through high pressure, which effectively utilizes calcined ash and calcined bottom ash as resources. It can also reduce the carbon dioxide generated by the use of cement powder in the product manufacturing process, so that calcined ash and calcined bottom ash can be fully utilized to achieve the purpose of sustainable development of resources.
接著,於此係舉下列實際範例說明以本實施例之應用混燒灰渣製備地磚之方法之該地磚之實施態樣。 Next, the following practical example is given to illustrate the implementation of the method of preparing floor tiles using mixed-burning ash in this embodiment.
實施例A: Embodiment A:
該攪拌比例:該混燒灰20Wt%、該爐石粉20Wt%、該天然砂60Wt%、該混燒底渣0Wt%;該第一時間:2分鐘(該混燒灰、該爐石粉、該天然砂及該混燒底渣之混拌時間);該液固比:0.21;該第二時間:3分鐘(該混合底料與該鹼性溶液之混拌時間);以及該壓力:80Kgf/cm2。 The mixing ratio is: 20 wt% of the mixed ash, 20 wt% of the furnace stone powder, 60 wt% of the natural sand, and 0 wt% of the mixed bottom ash; the first time is 2 minutes (mixing time of the mixed ash, the furnace stone powder, the natural sand, and the mixed bottom ash); the liquid-solid ratio is 0.21; the second time is 3 minutes (mixing time of the mixed bottom material and the alkaline solution); and the pressure is 80 Kgf/ cm2 .
實施例B: Embodiment B:
該攪拌比例:該混燒灰40Wt%、該爐石粉20Wt%、該天然砂40Wt%、該混燒底渣0Wt%;該第一時間:2分鐘(該混燒灰、該爐石粉、該天然砂及該混燒底渣之混拌時間); 該液固比:0.29;該第二時間:3分鐘(該混合底料與該鹼性溶液之混拌時間);以及該壓力:80Kgf/cm2。 The mixing ratio is: 40 wt% of the mixed ash, 20 wt% of the furnace stone powder, 40 wt% of the natural sand, and 0 wt% of the mixed bottom ash; the first time is 2 minutes (mixing time of the mixed ash, the furnace stone powder, the natural sand and the mixed bottom ash); the liquid-solid ratio is 0.29; the second time is 3 minutes (mixing time of the mixed bottom material and the alkaline solution); and the pressure is 80 Kgf/ cm2 .
實施例C: Embodiment C:
該攪拌比例:該混燒灰20Wt%、該爐石粉20Wt%、該天然砂0Wt%、該混燒底渣60Wt%;該第一時間:2分鐘(該混燒灰、該爐石粉、該天然砂及該混燒底渣之混拌時間);該液固比:0.23;該第二時間:3分鐘(該混合底料與該鹼性溶液之混拌時間);以及該壓力:80Kgf/cm2。 The mixing ratio is: 20 wt% of the mixed ash, 20 wt% of the furnace stone powder, 0 wt% of the natural sand, and 60 wt% of the mixed bottom ash; the first time is 2 minutes (mixing time of the mixed ash, the furnace stone powder, the natural sand and the mixed bottom ash); the liquid-solid ratio is 0.23; the second time is 3 minutes (mixing time of the mixed bottom material and the alkaline solution); and the pressure is 80 Kgf/ cm2 .
實施例D: Embodiment D:
該攪拌比例:該混燒灰10Wt%、該爐石粉20Wt%、該天然砂60Wt%、該混燒底渣10Wt%;該第一時間:2分鐘(該混燒灰、該爐石粉、該天然砂及該混燒底渣之混拌時間);該液固比:0.22;該第二時間:3分鐘(該混合底料與該鹼性溶液之混拌時間);以及該壓力:80Kgf/cm2。 The mixing ratio is: 10 wt% of the mixed ash, 20 wt% of the furnace stone powder, 60 wt% of the natural sand, and 10 wt% of the mixed bottom ash; the first time is 2 minutes (mixing time of the mixed ash, the furnace stone powder, the natural sand, and the mixed bottom ash); the liquid-solid ratio is 0.22; the second time is 3 minutes (mixing time of the mixed bottom material and the alkaline solution); and the pressure is 80 Kgf/ cm2 .
藉由上述之實施例A、實施例B、實施例C以及實施例D所制得之該地磚,進行熱壓膨脹分析,依據國家標準CNS1258規範之規定,目的在求得水泥砂漿之膨脹係數,試驗所用之儀器為高壓蒸煮鍋及量測水泥砂漿長度變化的比較側長儀;高壓蒸煮鍋即高壓蒸氣爐裝有自動壓力控制器並設有安全閥,從開始加壓時起在45~75分鐘內鍋爐內之壓力會到達規範之指定壓力20.8kgf/cm2,並維持至少三小時,蒸煮結束後將試體取出,於15分鐘內使水溫降至23度,保持試體及水在此溫度15分鐘,然後量其長度變化,其分析結果如下表一。 The floor tiles prepared by the above-mentioned embodiments A, B, C and D were subjected to hot pressure expansion analysis in accordance with the provisions of the national standard CNS1258, with the purpose of obtaining the expansion coefficient of cement mortar. The test instruments used were a high-pressure steam boiler and a comparative side length meter for measuring the length change of cement mortar; the high-pressure steam boiler is a high-pressure steam furnace equipped with an automatic pressure The pressure controller is also equipped with a safety valve. From the beginning of pressurization, the pressure in the boiler will reach the specified pressure of 20.8kgf/cm2 within 45 to 75 minutes and maintain it for at least three hours. After the steaming is completed, the sample is taken out and the water temperature is reduced to 23 degrees within 15 minutes. The sample and water are kept at this temperature for 15 minutes, and then the length change is measured. The analysis results are shown in Table 1 below.
實施例A、實施例B、實施例C以及實施例D該地磚之分別之熱壓膨脹分析如上表一所述之,其中,個別的實施例之該磚體雖然均有膨脹,但均 無破裂之現象發生,且膨脹率也都有低於規範限制值0.8%,因此以本發明製作出之該地磚係符合國家標準CNS1258規範之規定。 The thermal expansion analysis of the floor tiles of Example A, Example B, Example C and Example D is as described in Table 1 above. Although the brick bodies of the individual examples all expand, no cracking occurs, and the expansion rate is also lower than the standard limit of 0.8%. Therefore, the floor tiles made by the present invention meet the requirements of the national standard CNS1258.
以上所述之實施例,本發明係為一種應用混燒灰渣製備地磚之方法,使用爐石粉作為無機聚合技術之原料,搭配天然砂及鹼性溶液並以混燒灰及混燒底渣取代天然砂後進行混拌,透過高壓製成磚體,有效將混燒灰及混燒底渣進行資源化運用,更可以於產品製作過程減少使用水泥粉所產生之二氧化碳。 The above-mentioned embodiments are a method for preparing floor tiles using calcined ash and slag, using furnace stone powder as the raw material of inorganic polymerization technology, mixing with natural sand and alkaline solution, and replacing natural sand with calcined ash and calcined bottom slag, and then making bricks through high pressure, effectively making use of calcined ash and calcined bottom slag as resources, and reducing the carbon dioxide generated by cement powder in the product manufacturing process.
故本發明實為一具有新穎性、進步性及可供產業上利用者,應符合我國專利法專利申請要件無疑,爰依法提出發明專利申請,祈 鈞局早日賜准專利,至感為禱。 Therefore, this invention is novel, progressive and can be used in the industry. It should undoubtedly meet the patent application requirements of the Patent Law of our country. Therefore, I have filed an invention patent application in accordance with the law. I hope that the Bureau will approve the patent as soon as possible. I am very grateful.
惟以上所述者,僅為本發明之較佳實施例而已,並非用來限定本發明實施之範圍,舉凡依本發明申請專利範圍所述之形狀、構造、特徵及精神所為之均等變化與修飾,均應包括於本發明之申請專利範圍內。 However, the above is only a preferred embodiment of the present invention and is not intended to limit the scope of implementation of the present invention. All equivalent changes and modifications made according to the shape, structure, features and spirit described in the patent application scope of the present invention should be included in the patent application scope of the present invention.
S10:步驟 S10: Step
S20:步驟 S20: Step
S30:步驟 S30: Step
S40:步驟 S40: Step
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