TWI669281B - Humidity control ceramic and manufacturing method thereof - Google Patents
Humidity control ceramic and manufacturing method thereof Download PDFInfo
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Abstract
一種調濕陶瓷,其可包含焚化反應灰、玻璃、坡縷石及高嶺土。焚化反應灰之重量百分比可為5~20wt%。玻璃之重量百分比可為60~75wt%。坡縷石之重量百分比可為10~20wt%。高嶺土之重量百分比可為10~20wt%。 A humidity-conditioning ceramic may include incineration reaction ash, glass, palygorskite, and kaolin. The weight percentage of the incineration reaction ash may be 5-20% by weight. The weight percentage of glass can be 60 ~ 75wt%. The weight percentage of palygorskite can be 10-20% by weight. The weight percentage of kaolin can be 10-20 wt%.
Description
本發明係有關於一種調濕陶瓷,特別是一種環保調濕陶瓷。本發明還涉及此調濕陶瓷之製造方法。 The invention relates to a humidity-controlling ceramic, in particular to an environment-friendly humidity-controlling ceramic. The invention also relates to a method for manufacturing the humidity-conditioning ceramic.
為了能夠減少垃圾的體積,大部份的都市垃圾需經過焚化處理;經過焚化處理後,垃圾的體積約可降至原來的1/5,因此焚化法為目前主流的垃圾處理方式。然而,經過焚化法處理後的產生的焚化飛灰仍需經適當處理後才可進行最終掩埋,而對於人口密集的都市來說,可做為掩埋場的地點不易找尋;因此如何將焚化法處理後產生的焚化飛灰回收利用為一個重要的議題。 In order to reduce the volume of garbage, most of the municipal garbage needs to be incinerated; after the incineration, the volume of the garbage can be reduced to about 1/5 of the original. Therefore, incineration is the mainstream waste treatment method. However, the incineration fly ash generated after the incineration method still needs to be properly treated before it can be finally buried. For densely populated cities, the place that can be used as a landfill is not easy to find; therefore, how to deal with the incineration method The recycling of incinerated fly ash is an important issue.
都市垃圾焚化廠之空污控制設備所產生的焚化飛灰可分為焚化鍋爐灰及焚化反應灰;其中,焚化反應灰的重金屬含量極高,屬於有害廢棄物,因此極難以進行回收利用。 The incineration fly ash produced by the air pollution control equipment of the municipal waste incineration plant can be divided into incineration boiler ash and incineration reaction ash; among them, the incineration reaction ash has extremely high heavy metal content and belongs to hazardous waste, so it is extremely difficult to recycle.
目前已有幾種焚化飛灰回收再利用的技術提出,如中華民國專利申請號第104142783及中華民國專利申請號第102149264。然而,這些現有技術僅能回收利用焚化鍋爐灰,並無法有效針對焚化反應灰進行回收利用,因此焚化反應灰仍無法得到妥善的處理。 At present, several technologies for recycling incinerated fly ash have been proposed, such as the Republic of China Patent Application No. 104142783 and the Republic of China Patent Application No. 102149264. However, these existing technologies can only recycle the incineration boiler ash, and cannot effectively recycle the incineration reaction ash, so the incineration reaction ash cannot be properly processed.
因此,如何提出一種技術,能夠有效改善目前焚化反應灰無法有效地回收利用的情況已成為一個刻不容緩的問題。 Therefore, how to propose a technology that can effectively improve the current situation that incineration reaction ash cannot be effectively recycled has become an urgent issue.
本發明之實施例就是在提供一種調濕陶瓷及其製造方法,以解決目前焚化反應灰無法有效地回收利用的問題。 An embodiment of the present invention is to provide a humidity-controlling ceramic and a manufacturing method thereof to solve the problem that the incineration reaction ash cannot be effectively recycled.
根據本發明之其中一實施例,提出一種調濕陶瓷,其可包含焚化反應灰、玻璃、坡縷石及高嶺土。焚化反應灰之重量百分比可為5~20wt%。玻璃之重量百分比可為60~75wt%。坡縷石之重量百分比可為10~20wt%。高嶺土之重量百分比可為10~20wt%。 According to one embodiment of the present invention, a humidity-controlling ceramic is proposed, which may include incineration reaction ash, glass, palygorskite, and kaolin. The weight percentage of the incineration reaction ash may be 5-20% by weight. The weight percentage of glass can be 60 ~ 75wt%. The weight percentage of palygorskite can be 10-20% by weight. The weight percentage of kaolin can be 10-20 wt%.
在一實施例中,調濕陶瓷之吸濕量可在72g/m2以上。 In one embodiment, the moisture absorption capacity of the humidity-controlling ceramic can be more than 72 g / m 2 .
在一實施例中,調濕陶瓷之放濕率可在70%以上。 In one embodiment, the humidity release rate of the humidity-controlling ceramic can be more than 70%.
在一實施例中,調濕陶瓷之抗彎強度可在6.12MPa以上。 In one embodiment, the flexural strength of the humidity-controlling ceramic can be above 6.12 MPa.
根據本發明之其中一實施例,再提出一種調濕陶瓷之製造方法,其可包含下列步驟:提供焚化反應灰、玻璃、坡縷石及高嶺土,焚化反應灰之重量百分比為5~20wt%,玻璃之重量百分比為60~75wt%,坡縷石之重量百分比為10~20wt%,高嶺土之重量百分比為10~20wt%;混合焚化反應灰與坡縷石以產生混合物;執行濕式研磨程序研磨混合物;將玻璃、高嶺土及混合物混合並壓製成生胚;以及;執行燒結程序以產生調濕陶瓷。 According to one embodiment of the present invention, a method for manufacturing a humidity-controlling ceramic is further provided, which may include the following steps: providing incineration reaction ash, glass, palygorskite, and kaolin, the weight percentage of the incineration reaction ash is 5-20 wt%, The weight percentage of glass is 60 ~ 75% by weight, the weight percentage of palygorskite is 10-20% by weight, and the weight percentage of kaolin is 10-20% by weight; the incineration reaction ash and palygorskite are mixed to produce a mixture; wet grinding is performed A mixture; mixing and pressing glass, kaolin, and the mixture into a green body; and; performing a sintering procedure to produce a humidity-conditioning ceramic.
在一實施例中,混合焚化反應灰與坡縷石以產生混合物之步驟更包含下列步驟:執行水萃前處理程序對焚化反應灰進行前處理。 In one embodiment, the step of mixing the incineration reaction ash with palygorskite to generate a mixture further includes the following steps: performing a water extraction pretreatment procedure to pre-process the incineration reaction ash.
在一實施例中,混合焚化反應灰與坡縷石以產生混合物之步驟更包含下列步驟:將經過水萃前處理程序之焚化反應灰與坡縷石以1:1至1:2之比例混合。 In one embodiment, the step of mixing the incineration reaction ash and palygorskite to produce a mixture further comprises the following steps: mixing the incineration reaction ash and palygorskite which have undergone the water extraction pretreatment process in a ratio of 1: 1 to 1: 2 .
在一實施例中,燒結程序之溫度可為700℃~1000℃。 In one embodiment, the temperature of the sintering process may be 700 ° C to 1000 ° C.
在一實施例中,燒結程序之升溫速度可為1℃~30℃/min。 In one embodiment, the heating rate of the sintering process may be 1 ° C to 30 ° C / min.
在一實施例中,壓製生胚之成型壓力可為1900-2100psi。 In one embodiment, the forming pressure of the pressed green embryo can be 1900-2100 psi.
為讓本發明的上述特徵和特性能更明顯易懂,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 features and characteristics of the present invention more comprehensible, embodiments are described below in detail with reference to the accompanying drawings.
S11~S15、S21~S26‧‧‧步驟流程 S11 ~ S15, S21 ~ S26‧‧‧step flow
第1圖 係為本發明之調濕陶瓷之製造方法之一實施例之流程圖。 FIG. 1 is a flowchart of an embodiment of a method for manufacturing a humidity-controlling ceramic according to the present invention.
第2圖 係為本發明之調濕陶瓷之製造方法之一實施例之流程圖。 FIG. 2 is a flowchart of an embodiment of a method for manufacturing a humidity-controlling ceramic according to the present invention.
以下將參照相關圖式,說明依本發明之調濕陶瓷及其製造方法之實施例,為了清楚與方便圖式說明之故,圖式中的各部件在尺寸與比例上可能會被誇大或縮小地呈現。在以下描述及/或申請專利範圍中,當提及元件「連接」或「耦合」至另一元件時,其可直接連接或耦合至該另一元件或可存在介入元件;而當提及元件「直接連接」或「直接耦合」至另一元件時,不存在介入元件,用於描述元件或層之間之關係之其他字詞應以相同方式解釋。為使便於理解,下述實施例中之相同元件係以相同之符號標示來說明。 In the following, embodiments of the humidity-controlling ceramic and its manufacturing method according to the present invention will be described with reference to related drawings. For clarity and convenience of illustration, the components in the drawings may be exaggerated or reduced in size and proportion. To present. In the following description and / or patent application, when an element is referred to as being "connected" or "coupled" to another element, it can be directly connected or coupled to the other element or intervening elements may be present; and when an element is referred to When "directly connected" or "directly coupled" to another element, there are no intervening elements present, and other words used to describe the relationship between elements or layers should be interpreted the same way. In order to facilitate understanding, the same elements in the following embodiments are described with the same symbols.
請參閱表1,其係為本發明之調濕陶瓷之實施例之成份組成表,如下:
由表1可知,本實施例之調濕陶瓷可包含焚化反應灰、玻璃(廢棄玻璃)、坡縷石及高嶺土等四種成份。 As can be seen from Table 1, the humidity-controlling ceramics of this embodiment may include four components such as incineration reaction ash, glass (waste glass), palygorskite, and kaolin.
其中,焚化反應灰之重量百分比可為5~20wt%。玻璃之重量百分比可為60~75wt%。坡縷石之重量百分比可為10~20wt%。高嶺土之重量百分比 可為10~20wt%。 The weight percentage of the incineration reaction ash may be 5-20 wt%. The weight percentage of glass can be 60 ~ 75wt%. The weight percentage of palygorskite can be 10-20% by weight. Kaolin weight percentage It can be 10 ~ 20wt%.
在本實施例中,調濕陶瓷可利用包含焚化反應灰、玻璃、坡縷石及高嶺土等四種成份的特殊成份組成及比例,且焚化反應灰之重量百分比最高可高達20%,使焚化反應灰可以得到妥善的處理。另外,調濕陶瓷之玻璃之重量百分比也佔了極高的比例,因此,廢棄玻璃也可以得到有效地回收利用。 In this embodiment, the humidity-controlling ceramic can use the special composition and ratio of four components including incineration reaction ash, glass, palygorskite, and kaolin, and the weight percentage of incineration reaction ash can be as high as 20%, so that the incineration reaction Ash can be properly disposed of. In addition, the weight percentage of the glass of the humidity-controlling ceramics also accounts for a very high proportion, so the waste glass can also be effectively recycled.
其中,為了有效地穩定焚化反應灰內之重金屬,以防止其溶出,本實施例可先將焚化反應灰與坡縷石混合以產生混合物,再可進一步採取濕式研磨程序研磨此混合物以有效地穩定焚化反應灰內之重金屬。透過上述特殊的濕式研磨穩定程序,重金屬溶出即可遠低於焚化灰渣再利用標準之限值。 Among them, in order to effectively stabilize the heavy metals in the incineration reaction ash to prevent its dissolution, in this embodiment, the incineration reaction ash and palygorskite can be mixed to produce a mixture, and then the wet grinding process can be used to grind the mixture to effectively Stable incineration of heavy metals in reaction ash. Through the above-mentioned special wet grinding stabilization procedure, heavy metal dissolution can be far below the limit of the incineration ash reuse standard.
接下來,可將玻璃、高嶺土及混合物混合並壓製成生胚,最後再執行燒結程序以產生調濕陶瓷。 Next, the glass, kaolin, and the mixture can be mixed and pressed into a green body, and finally a sintering process is performed to produce a humidity-conditioning ceramic.
透過上述的製造方法,本實施例之調濕陶瓷之吸濕量可達到72g/m2以上、放濕率可達到70%以上,而抗彎強度可達到6.12MPa以上,燒結溫度 可降低到1000℃以下。 Through the above-mentioned manufacturing method, the moisture absorption capacity of the humidity-controlling ceramic of this embodiment can reach more than 72 g / m 2 , the moisture release rate can reach more than 70%, and the bending strength can reach more than 6.12 MPa, and the sintering temperature can be reduced to 1000. Below ℃.
因此,由上述可知,本實施例之調濕陶瓷確實可以有效地回收利用焚化反應灰,使有害廢棄物可以再生利用為高經濟價值的產品,確實改善了習知技藝之缺點。 Therefore, from the above, it can be known that the humidity-controlling ceramic of this embodiment can effectively recycle the incineration reaction ash, so that harmful waste can be recycled into a product with high economic value, and the shortcomings of the conventional technique are improved.
值得一提的是,現有的幾種焚化飛灰回收再利用的技術僅能回收利用焚化鍋爐灰,並無法有效針對焚化反應灰進行回收利用,因此焚化反應灰仍無法得到妥善的處理。相反的,根據本發明之實施例,調濕陶瓷之成份可包含焚化反應灰,且焚化反應灰之重量百分比可高達5~20wt%,因此可以對有效地回收利用焚化反應灰,使焚化反應灰可以得到妥善的處理。 It is worth mentioning that several existing incineration fly ash recovery and reuse technologies can only recycle incineration boiler ash and cannot effectively recycle the incineration reaction ash, so the incineration reaction ash cannot be properly treated. In contrast, according to the embodiment of the present invention, the components of the humidity-controlling ceramic may include incineration reaction ash, and the weight percentage of the incineration reaction ash may be as high as 5 to 20% by weight. Therefore, the incineration reaction ash can be effectively recycled and used to make the incineration reaction ash effective. Can be properly handled.
又,根據本發明之實施例,在調濕陶瓷的製程中採用特殊的濕式研磨程序,其可以有效地穩定焚化反應灰內之重金屬使其符合標準,使調濕陶瓷能夠更加的穩定安全。 In addition, according to the embodiment of the present invention, a special wet grinding process is adopted in the process of humidity-controlling ceramics, which can effectively stabilize the incineration of heavy metals in the reaction ash to meet standards, so that the humidity-controlling ceramics can be more stable and safe.
此外,根據本發明之實施例,調濕陶瓷之吸濕量可達到72g/m2以上,放濕率可達到70%以上,而抗彎強度可達到6.12MPa以上,燒結溫度可降低到1000℃以下,因此具有極佳的性能。 In addition, according to the embodiment of the present invention, the moisture absorption capacity of the humidity-adjusting ceramic can reach 72 g / m 2 or more, the moisture release rate can reach 70% or more, the bending strength can reach 6.12 MPa or more, and the sintering temperature can be reduced to 1000 ° C. Below, it has excellent performance.
另外,根據本發明之實施例,調濕陶瓷之燒結程序之溫度可在1000℃以下,因此使調濕陶瓷能具有更佳的特性,且同時其成本也能夠進一步降低。 In addition, according to the embodiment of the present invention, the temperature of the sintering procedure of the humidity-controlling ceramic can be below 1000 ° C., so that the humidity-controlling ceramic can have better characteristics, and at the same time, its cost can be further reduced.
再者,根據本發明之實施例,調濕陶瓷可大量應用於建築物中,且由於具有極佳的性能,故可有效提升人體健康並改善居家環境,因此應用上極為廣泛。由上述可知,本發明極具進步性之專利要件。 Furthermore, according to the embodiments of the present invention, humidity-controlling ceramics can be widely used in buildings, and because of their excellent performance, they can effectively improve human health and improve the home environment, so they are widely used. As can be seen from the above, the present invention has extremely advanced patent requirements.
請參閱第1圖,其係為本發明之調濕陶瓷之製造方法之一實施例之流程圖。本實施例之調濕陶瓷之製造方法可含下列步驟: Please refer to FIG. 1, which is a flowchart of an embodiment of a method for manufacturing a humidity-controlling ceramic according to the present invention. The manufacturing method of the humidity-controlling ceramic in this embodiment may include the following steps:
步驟S11:提供焚化反應灰、玻璃、坡縷石及高嶺土,焚化反應灰之重 量百分比為5~20wt%,玻璃之重量百分比為60~75wt%,坡縷石之重量百分比為10~20wt%,及高嶺土之重量百分比為10~20wt%。 Step S11: Provide incineration reaction ash, glass, palygorskite and kaolin, and weight of incineration reaction ash The amount percentage is 5 to 20% by weight, the weight percentage of glass is 60 to 75% by weight, the weight percentage of palygorskite is 10 to 20% by weight, and the weight percentage of kaolin is 10 to 20% by weight.
步驟S12:混合焚化反應灰與坡縷石以產生混合物。 Step S12: Mix the incineration reaction ash with palygorskite to produce a mixture.
步驟S13:執行濕式研磨程序研磨混合物。 Step S13: The wet grinding process is performed to grind the mixture.
步驟S14:將混合物與玻璃及高嶺土混合並壓製成生胚。 Step S14: The mixture is mixed with glass and kaolin and pressed into a green embryo.
步驟S15:執行燒結程序以產生調濕陶瓷。 Step S15: A sintering process is performed to produce a humidity-conditioning ceramic.
上述僅為舉例,調濕陶瓷之成份及其製造方法均可依實際需求變化,本發明並不以此為限。 The above is only an example. The ingredients of the humidity-controlling ceramics and the manufacturing method thereof can be changed according to actual needs, and the present invention is not limited thereto.
請參閱第2圖,其係為本發明之調濕陶瓷之製造方法之一實施例之流程圖。本實施例舉例說明了調濕陶瓷之製造方法之詳細內容。 Please refer to FIG. 2, which is a flowchart of an embodiment of a method for manufacturing a humidity-controlling ceramic according to the present invention. This embodiment illustrates the details of the manufacturing method of the humidity-controlling ceramic.
如前述,本實施例之調濕陶瓷可包含焚化反應灰、玻璃(廢棄玻璃)、坡縷石及高嶺土等四種成份。其中,焚化反應灰之重量百分比可為5~20wt%。玻璃之重量百分比可為60~75wt%。坡縷石之重量百分比可為10~20wt%。高嶺土之重量百分比可為10~20wt%。 As mentioned above, the humidity-controlling ceramic of this embodiment may include four components such as incineration reaction ash, glass (waste glass), palygorskite, and kaolin. The weight percentage of the incineration reaction ash may be 5-20 wt%. The weight percentage of glass can be 60 ~ 75wt%. The weight percentage of palygorskite can be 10-20% by weight. The weight percentage of kaolin can be 10-20 wt%.
其中,本實施例之上述原料可透過適當的前處理再進行後續的程序。其中,玻璃可利用廢棄玻璃,並去除標籤、清洗、烘乾及破碎,再可透過顎碎機破碎成更小的細粉後過篩備用。 Wherein, the above-mentioned raw materials in this embodiment may be subjected to an appropriate pre-treatment before performing subsequent procedures. Among them, the glass can use waste glass, and can be removed from the label, washed, dried and broken, and then can be broken into smaller fine powder by the jaw crusher and then sieved for use.
本實施例之焚化反應灰可透過水萃前處理以去除對重金屬穩定及燒結體耐久性不利的鹽類;在本實施例中,操作條件液固為5,萃取時間為5分鐘,次數為2次,水萃後之焚化反應灰經固液分離後,取濾餅烘乾、冷卻、破碎後粉體密封於容器以備用。 The incineration reaction ash of this embodiment can be subjected to water extraction pretreatment to remove salts that are unfavorable to the stability of heavy metals and the durability of the sintered body. In this embodiment, the operating conditions are liquid solids, extraction time is 5 minutes, and the number is 2 Secondly, after the water-extraction incineration reaction ash is separated by solid-liquid, the filter cake is taken to dry, cool, and crushed, and the powder is sealed in a container for future use.
本實施例之高嶺土可採用工業級之高嶺土,並確保其乾燥,且儲存於密封罐以備用 The kaolin in this embodiment can be industrial grade kaolin, and ensure that it is dry and stored in a sealed tank for future use.
本實施例之坡縷石可採用工業級坡縷石,經高溫活化程序之前處理, 並以400℃之溫度持續處理4小時,再冷卻、破碎後將粉體密封於容器中以備用。 The palygorskite in this embodiment may be industrial-grade palygorskite, which is processed before the high-temperature activation procedure. And the treatment was continued at a temperature of 400 ° C for 4 hours. After cooling and crushing, the powder was sealed in a container for future use.
當然,上述各項條件均為舉例說明而已,各原料之前處理程序可依實際需求變化,本發明並不以此為限。 Of course, the above conditions are just examples, and the pre-treatment procedures for each raw material can be changed according to actual needs, and the present invention is not limited thereto.
本實施例可採用特殊的濕式研磨程序,其可以有效地穩定焚化反應灰內之重金屬。本實施例採用普通球磨機及氧化鋁研磨球做為研磨設備,而研磨參數為:濕式研磨液固比為重量比9:1;轉速為86rpm;研磨時間為2小時;其中,進行此濕式研磨程序時,可將經過水萃前處理程序之焚化反應灰與坡縷石以1:1至1:2之比例混合。 In this embodiment, a special wet grinding process can be adopted, which can effectively stabilize the heavy metals in the incineration reaction ash. This embodiment uses ordinary ball mills and alumina grinding balls as grinding equipment, and the grinding parameters are: wet grinding liquid-solid ratio is 9: 1 by weight; rotation speed is 86 rpm; grinding time is 2 hours; among them, the wet During the grinding process, the incineration reaction ash and palygorskite which have undergone the water extraction pretreatment process can be mixed in a ratio of 1: 1 to 1: 2.
然後,將玻璃、高嶺土及混合物混合並壓製成生胚,其成型壓力可為1,900-2,100psi;在本實施中,成型壓力可為2,000psi;成型後放入105℃之烘箱中烘乾,以確保生胚的形狀完整性;在本實施例中,生胚的尺寸大小為長10公分、寬5公分及厚0.5公分。 Then, the glass, kaolin and the mixture are mixed and pressed into a green embryo, and the molding pressure can be 1,900-2,100 psi; in this implementation, the molding pressure can be 2,000 psi; after molding, it is dried in an oven at 105 ° C. The shape integrity of the green embryo is ensured; in this embodiment, the size of the green embryo is 10 cm in length, 5 cm in width, and 0.5 cm in thickness.
最後可進行燒結程序,調濕陶瓷之製造方法可採用較低的溫度,約為700℃~1,000℃;本實施例分別採用800℃、850℃、900℃及950℃,升溫速度為1℃~30℃/min,持溫5分鐘後自然降至室溫,而採用的燒結設備為高溫矩形爐之空氣氣氛燒結。 Finally, the sintering process can be performed. The manufacturing method of the humidity-controlling ceramics can use a lower temperature, about 700 ° C to 1,000 ° C. This embodiment uses 800 ° C, 850 ° C, 900 ° C, and 950 ° C, and the heating rate is 1 ° C ~ 30 ℃ / min, it will naturally drop to room temperature after 5 minutes of holding temperature, and the sintering equipment used is air atmosphere sintering of high temperature rectangular furnace.
當然,上述各項條件均為舉例說明而已,各項條件可依實際需求變化,本發明並不以此為限。 Of course, the above conditions are only examples, and the conditions may be changed according to actual needs, and the present invention is not limited thereto.
首先,本實施例針對燒結體之機械特性,包含燒失率、體積變化率及抗彎強度。其中,抗彎強度為調濕陶瓷機械特性最重要的品質指標;分析燒失率可知道在不同的溫度及燒結條件下重量損失情形;分析體積變化率可了解燒結前後的尺寸變化,其影響燒結試體之強度及吸放濕效果。 First, the mechanical characteristics of the sintered body in this embodiment include the loss on ignition rate, volume change rate, and flexural strength. Among them, the bending strength is the most important quality index of the mechanical properties of humidity-controlling ceramics; the loss of ignition rate can be used to know the weight loss at different temperatures and sintering conditions; the volume change rate can be used to understand the dimensional change before and after sintering, which affects sintering Specimen strength and moisture absorption and release effect.
分析結果如表2所示,其中玻璃、焚化反應灰、高嶺土及坡縷石分別
以大寫字母G、F、K及P,而其重量百分比以數字表示;如GFKP-6112表示玻璃之重量百分比為60%,焚化反應灰之重量百分比為10%,高嶺土之重量百分比為10%,而坡縷石之重量百分比為20%;另外,體積變化率正值為膨脹,負值為收縮,數據表示為平均值±標準差,如下:
由表2可知,本實施例顯示包含玻璃、焚化反應灰、高嶺土及坡縷石等四種成份的GFKP-6211、GFKP-6121、GFKP-6112,其使用濕式研磨程序將焚化反應灰與坡縷石共同研磨可有效穩定焚化反應灰之重金屬及其粉體物化性質,再透過玻璃及高嶺土的適當調質並控制適當的燒結條件下可成功燒製高性能之環保調濕陶瓷。 As can be seen from Table 2, this example shows GFKP-6211, GFKP-6121, and GFKP-6112 containing four components including glass, incineration reaction ash, kaolin, and palygorskite. The wet incineration reaction ash and slope are used in the process The co-grinding of whirlite can effectively stabilize the physicochemical properties of the heavy metals and powders of the incineration reaction ash, and then, through proper tempering of glass and kaolin and control of appropriate sintering conditions, high-performance environmentally friendly humidity-controlling ceramics can be successfully fired.
與僅使用三種成份的GFKP-6220、GFKP-6202、GFKP-6130及GFKP-6103相較,在高溫燒結的條件下,GFKP-6211、GFKP-6121及GFKP-6112也能具有極佳的抗彎強度。 Compared with GFKP-6220, GFKP-6202, GFKP-6130, and GFKP-6103, which use only three ingredients, GFKP-6211, GFKP-6121, and GFKP-6112 also have excellent bending resistance under high temperature sintering conditions. strength.
在本實施例中,透過上述之方法製造調濕陶瓷,並利用JIS A 1470-1調濕建材的吸放濕性試驗方法-第1部份:濕度應答法-濕度變動的吸放濕方法來進行測試,再以下列式(1)~(3)計算:Wa=(Ma-M0)/A......................................................................(1) In this example, a humidity-controlling ceramic is manufactured by the method described above, and JIS A 1470-1 is used to test the moisture absorption and release properties of building materials-Part 1: Humidity Response Method-Humidity Change Method Test it and calculate it with the following formulas (1) ~ (3): W a = (M a -M 0 ) / A ............ ................................................(1 )
Wd=(ma-m1)/A......................................................................(2) W d = (m a -m 1 ) / A ............ ................................(2)
Ws=Ma-Md...........................................................................(3) W s = M a -M d ............... ....................... (3)
其中,Wa表示吸濕過程終了時之吸濕量(g/m2);Wd表示放濕過程終了時之放濕量(g/m2);Ws殘留水分量(g/m2);ma表示吸濕過程終了時之試體之質量(g);md表示放濕過程終了時之試體之質量(g);m0養生後試體的質量(g);A表示接觸面面積(m2)。調濕性能分析結果如表3所示,其中標示「*」調濕性能符合第三級標準(70%)以上(本實施例採用日本調濕建材調濕性能評價基準),如下:表3 不同成份之調濕陶瓷之調濕性能表
由上表可知,本實施例顯示包含玻璃、焚化反應灰、高嶺土及坡縷石等四種成份的GFKP-6121及GFKP-6112在850℃的低溫燒結條件下已可達到最高品質的第三級標準,同時也可符合CNS陶瓷面磚抗彎強度要求。 As can be seen from the table above, this example shows that GFKP-6121 and GFKP-6112 containing four components including glass, incineration reaction ash, kaolin, and palygorskite can reach the third grade of the highest quality under low temperature sintering conditions of 850 ° C. The standard can also meet the bending strength requirements of CNS ceramic tiles.
表4表示不同成份之調濕陶瓷之燒結體毒性溶出試驗,其中數據表示為平均值±標準差,而「N.D.」表示低於儀器偵測極限,如下:
由上表可知,本實施例顯示包含玻璃、焚化反應灰、高嶺土及坡縷石等四種成份的GFKP-6121及GFKP-6112在850℃的低溫燒結條件下也可符合焚化灰渣的再利用標準,根據經驗,如採還原氣氛燒結,重金屬鉻將遠低於該項標準。 As can be seen from the table above, this example shows that GFKP-6121 and GFKP-6112 containing four components including glass, incineration reaction ash, kaolin, and palygorskite can also meet the reuse of incinerated ash under low temperature sintering conditions at 850 ° C. Standard, according to experience, such as reducing atmosphere sintering, heavy metal chromium will be far below this standard.
由上述可知,本實施例之調濕陶瓷不但可具有極佳的性能,且調濕陶瓷之燒結程序之溫度可在850℃即可達到極佳的效果,因此其成本也能夠進一步降低。 It can be known from the foregoing that the humidity-controlling ceramic of this embodiment not only has excellent performance, but also the temperature of the sintering process of the humidity-controlling ceramic can achieve an excellent effect at 850 ° C, so its cost can be further reduced.
如圖所示,本實施例可包含下列步驟: As shown in the figure, this embodiment may include the following steps:
步驟S21:提供焚化反應灰、玻璃、坡縷石及高嶺土,焚化反應灰之重量百分比為5~20wt%,玻璃之重量百分比為60~75wt%,坡縷石之重量百分比為10~20wt%,及高嶺土之重量百分比為10~20wt%。 Step S21: Provide incineration reaction ash, glass, palygorskite and kaolin, the weight percentage of incineration reaction ash is 5-20% by weight, the weight percentage of glass is 60-75% by weight, and the weight percentage of palygorskite is 10-20% by weight. And the weight percentage of kaolin is 10 ~ 20wt%.
步驟S22:執行水萃前處理程序對焚化反應灰進行前處理。 Step S22: Perform a water extraction pre-treatment program to pre-treat the incineration reaction ash.
步驟S23:將經過水萃前處理程序之焚化反應灰與坡縷石以1:1至1:2之比例混合以產生混合物。 Step S23: Mix the incineration reaction ash and palygorskite which have undergone the water extraction pretreatment procedure in a ratio of 1: 1 to 1: 2 to produce a mixture.
步驟S24:執行濕式研磨程序研磨混合物。 Step S24: The wet grinding process is performed to grind the mixture.
步驟S25:將混合物與玻璃及高嶺土混合並以成型壓力1900-2100psi壓製成生胚。 Step S25: The mixture is mixed with glass and kaolin and pressed into a green embryo at a molding pressure of 1900-2100 psi.
步驟S26:執行燒結程序以產生調濕陶瓷,其中燒結程序之溫度為700℃~1000℃,且升溫速度為1℃~30℃/min。 Step S26: A sintering procedure is performed to generate a humidity-controlling ceramic, wherein the temperature of the sintering procedure is 700 ° C. to 1000 ° C., and the heating rate is 1 ° C. to 30 ° C./min.
上述僅為舉例,調濕陶瓷之成份及其製造方法均可依實際需求變化,本發明並不以此為限。 The above is only an example. The ingredients of the humidity-controlling ceramics and the manufacturing method thereof can be changed according to actual needs, and the present invention is not limited thereto.
綜合上述,根據本發明之實施例,調濕陶瓷之成份可包含焚化反應灰,且焚化反應灰之重量百分比可高達5~20wt%,因此可以對有效地回收利用焚化反應灰,使焚化反應灰可以得到妥善的處理。 To sum up, according to the embodiment of the present invention, the components of the humidity-controlling ceramic may include incineration reaction ash, and the weight percentage of the incineration reaction ash may be as high as 5 to 20% by weight. Therefore, the incineration reaction ash can be effectively recycled and the incineration reaction ash Can be properly handled.
又,根據本發明之實施例,在調濕陶瓷的製程中採用特殊的濕式研磨穩定程序,其可以有效地穩定焚化反應灰內之重金屬,使調濕陶瓷能夠更加的穩定安全。 In addition, according to the embodiment of the present invention, a special wet-grinding stabilization procedure is used in the process of humidity-controlling ceramics, which can effectively stabilize the heavy metals in the incineration reaction ash, so that the humidity-controlling ceramics can be more stable and safe.
此外,根據本發明之實施例,調濕陶瓷之吸濕量可達到72g/m2以上, 放濕率可達到70%以上,而抗彎強度可達到6.12MPa以上,燒結溫度可降低到1000℃以下,因此具有極佳的性能。 In addition, according to the embodiment of the present invention, the moisture absorption capacity of the humidity-adjusting ceramic can reach more than 72 g / m 2 , the moisture release rate can reach more than 70%, the bending strength can reach more than 6.12 MPa, and the sintering temperature can be reduced to 1000 ° C. Below, it has excellent performance.
另外,根據本發明之實施例,調濕陶瓷之燒結程序之溫度可在1000℃以下,因此使調濕陶瓷能具有更佳的特性,且同時其成本也能夠進一步降低。 In addition, according to the embodiment of the present invention, the temperature of the sintering procedure of the humidity-controlling ceramic can be below 1000 ° C., so that the humidity-controlling ceramic can have better characteristics, and at the same time, its cost can be further reduced.
再者,根據本發明之實施例,調濕陶瓷可大量應用於建築物中,且由於具有極佳的性能,故可有效提升人體健康並改善居家環境,因此應用上極為廣泛。 Furthermore, according to the embodiments of the present invention, humidity-controlling ceramics can be widely used in buildings, and because of their excellent performance, they can effectively improve human health and improve the home environment, so they are widely used.
可見本發明在突破先前之技術下,確實已達到所欲增進之功效,且也非熟悉該項技藝者所易於思及,其所具之進步性、實用性,顯已符合專利之申請要件,爰依法提出專利申請,懇請 貴局核准本件發明專利申請案,以勵創作,至感德便。 It can be seen that the present invention has indeed achieved the desired effect under the breakthrough of the previous technology, and it is not easy for those skilled in the art to think about, and its progressiveness and practicability obviously meet the requirements of patent application. I filed a patent application in accordance with the law, and kindly ask your office to approve this invention patent application in order to encourage creativity and to feel good.
以上所述僅為舉例性,而非為限制性者。其它任何未脫離本發明之精神與範疇,而對其進行之等效修改或變更,均應該包含於後附之申請專利範圍中。 The above description is exemplary only, and not restrictive. Any other equivalent modifications or changes made without departing from the spirit and scope of the present invention should be included in the scope of the attached patent application.
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