TWI568702B - Humidity controlling ceramics and preparation thereof - Google Patents

Humidity controlling ceramics and preparation thereof Download PDF

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TWI568702B
TWI568702B TW104142783A TW104142783A TWI568702B TW I568702 B TWI568702 B TW I568702B TW 104142783 A TW104142783 A TW 104142783A TW 104142783 A TW104142783 A TW 104142783A TW I568702 B TWI568702 B TW I568702B
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amount
humidity
weight
boiler ash
palygorskite
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TW104142783A
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TW201722882A (en
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高思懷
孫常榮
李明國
徐志緯
黃啓賓
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淡江大學
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    • 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
    • Y02P40/60Production of ceramic materials or ceramic elements, e.g. substitution of clay or shale by alternative raw materials, e.g. ashes

Description

調濕陶瓷及其製作方法 Humidity control ceramic and manufacturing method thereof

本發明是關於調濕陶瓷及其製作方法,特別是一種使用焚化鍋爐灰、廢棄玻璃及坡縷石製作的調濕陶瓷及其製作方法。 The invention relates to a humidity control ceramic and a preparation method thereof, in particular to a humidity control ceramic prepared by using incinerator boiler ash, waste glass and palygorskite and a preparation method thereof.

隨著人口的成長,所產生的大量垃圾已成為各國需要解決問題。由於焚化可以大量減少垃圾的體積,因而是垃圾處理的重要方法。然而,垃圾焚化所產生的大量焚化鍋爐灰仍需要進一步的掩埋處理,這又產生了新的環境影響。 As the population grows, the amount of garbage generated has become a problem that countries need to solve. Since incineration can greatly reduce the volume of garbage, it is an important method of garbage disposal. However, the large incineration of boiler ash from waste incineration still requires further landfill disposal, which in turn creates new environmental impacts.

另一方面,隨著環保意識的抬頭,目前也收集了大量的玻璃。目前這些玻璃主要是以堆積的方式放置,因而需要極大的容置空間,因而如何處理所回收的大量廢棄玻璃,也成為目前需要解決的問題。 On the other hand, with the rise of environmental awareness, a large amount of glass has been collected. At present, these glasses are mainly placed in a stacked manner, and thus require a large accommodation space, so how to deal with the large amount of discarded glass recovered is also a problem that needs to be solved at present.

如上所述,如何處理垃圾焚化所產生的大量焚化鍋爐灰以及所回收的廢棄玻璃,即成為目前研究人員所需解決的問題。 As mentioned above, how to deal with the large amount of incineration boiler ash generated by waste incineration and the recycled waste glass has become a problem that researchers need to solve.

為了解決先前技術中垃圾焚化所產生的大量焚化鍋爐灰以及所回收的廢棄玻璃,本發明提供一種使用焚化鍋爐灰、廢棄玻璃及坡縷石製作的調濕陶瓷及其製作方法,以有效利用焚化鍋爐灰及廢棄玻璃,並且製造一種具有較佳的吸濕效果的調濕陶瓷。 In order to solve the large amount of incineration boiler ash and waste glass recovered by waste incineration in the prior art, the present invention provides a humidity control ceramic prepared by using incinerator boiler ash, waste glass and palygorskite and a manufacturing method thereof for effectively utilizing incineration Boiler ash and waste glass, and a humidity-conditioning ceramic with better moisture absorption effect.

根據本發明一實施例所揭露之調濕陶瓷,其係按照下列比例加以混合燒結製成:一焚化鍋爐灰,焚化鍋爐灰的用量為5-60wt%;一廢棄玻璃,廢棄玻璃的用量為10-85wt%;以及一坡縷石,坡縷石的用量為10-60wt%。 According to an embodiment of the present invention, the humidity-regulating ceramic is prepared by mixing and sintering according to the following ratios: an incineration boiler ash, the amount of incineration boiler ash is 5 to 60 wt%; and a waste glass, the amount of waste glass is 10 -85 wt%; and a palygorskite, the amount of palygorskite is 10-60% by weight.

在一實施例中,焚化鍋爐灰的用量為10wt%,廢棄玻璃的用量為70wt%,坡縷石的用量為20wt%。 In one embodiment, the amount of incineration boiler ash is 10% by weight, the amount of waste glass is 70% by weight, and the amount of palygorskite is 20% by weight.

根據本發明一實施例所揭露之調濕陶瓷的製作方法,包含:進行一前處理步驟,包含:蒐集焚化鍋爐灰,將焚化鍋爐灰進行水萃處理,水萃處理後之焚化鍋爐灰經固液分離以形成一焚化鍋爐灰;進行一廢棄玻璃顎碎、篩分,以提供一廢棄玻璃;以及提供一坡縷石;將焚化鍋爐灰、廢棄玻璃及坡縷石混合以製成一生胚,其中,焚化鍋爐灰的用量為5-60wt%,廢棄玻璃的用量為10-85wt%坡縷石的用量為10-60wt%;以及將生胚執行一燒結程序。 A method for manufacturing a humidity-controlling ceramic according to an embodiment of the present invention comprises: performing a pre-treatment step comprising: collecting incineration boiler ash, performing water extraction treatment on the incinerator boiler ash, and incineration boiler ash solidification after water extraction treatment Separating the liquid to form an incinerator boiler ash; performing a waste glass mashing and sieving to provide a waste glass; and providing a palygorskite; mixing the incineration boiler ash, the waste glass and the palygorskite to form a green embryo, Wherein, the amount of the incinerator boiler ash is 5 to 60% by weight, the amount of the waste glass is 10 to 85% by weight, and the amount of the palygorskite is 10 to 60% by weight; and the sintering process is performed on the green embryo.

在一實施例中,焚化鍋爐灰的用量為10wt%,廢棄玻璃的用量為70wt%,坡縷石的用量為20wt%。 In one embodiment, the amount of incineration boiler ash is 10% by weight, the amount of waste glass is 70% by weight, and the amount of palygorskite is 20% by weight.

在一實施例中,於製成一生胚之步驟中,生坯的含水率為10~20wt%,生坯的含水率是以生胚之總重量為基準。 In one embodiment, in the step of forming a green embryo, the moisture content of the green body is 10 to 20% by weight, and the moisture content of the green body is based on the total weight of the green embryo.

在一實施例中,於製成一生胚之步驟中,生坯的含水率為15wt%,生坯的含水率是以生胚之總重量為基準。 In one embodiment, in the step of forming a green embryo, the moisture content of the green body is 15% by weight, and the moisture content of the green body is based on the total weight of the green embryo.

在一實施例中,於製成一生胚之步驟中,生胚是以2000psi之壓力壓製成型,且壓製時間為1分鐘。 In one embodiment, in the step of making a green embryo, the green embryo is press molded at a pressure of 2000 psi and the pressing time is 1 minute.

在一實施例中,燒結程序之燒結溫度為700℃~1000℃。 In one embodiment, the sintering temperature of the sintering process is from 700 ° C to 1000 ° C.

在一實施例中,燒結程序之升溫速率介於1~30℃/min。 In one embodiment, the sintering process has a ramp rate of between 1 and 30 ° C/min.

根據上述本發明所揭露之實施例,由於本發明是利用焚化鍋爐灰、廢棄玻璃及坡縷石製成調濕陶瓷,因而可成功將有害廢棄物回收利用,並且調濕陶瓷具有較佳的吸濕量、放濕率,並且可避免重金屬在製程中流出,是具有高經濟價值的環保高性能調濕陶瓷。 According to the embodiment of the present invention disclosed above, since the invention utilizes incineration boiler ash, waste glass and palygorskite to make a humidity-control ceramic, the hazardous waste can be successfully recycled, and the humidity-control ceramic has better suction. The moisture content, the moisture release rate, and the avoidance of heavy metals flowing out during the process are environmentally-friendly high-performance humidity-control ceramics with high economic value.

以上之關於本發明內容之說明及以下之實施方式之說明係用以示範與解釋本發明之原理,並且提供本發明之專利申請範圍更進一步之解釋。 The above description of the present invention and the following description of the embodiments of the present invention are intended to illustrate and explain the principles of the invention.

第1圖為本發明一實施例所製備之調濕陶瓷的製作方法之流程圖。 1 is a flow chart showing a method of fabricating a humidity-conditioning ceramic prepared according to an embodiment of the present invention.

第2圖為第1圖之前處理步驟之詳細流程圖。 Figure 2 is a detailed flow chart of the processing steps before Figure 1.

第3圖為本發明實施例之調濕陶瓷在不同燒結溫度的吸放濕試驗。 Figure 3 is a graph showing the moisture absorption and desorption test of the humidity-conditioning ceramics at different sintering temperatures according to an embodiment of the present invention.

第4A圖至第4C圖分別為本發明實施例之調濕陶瓷在不同燒結溫度的SEM分析結果。 4A to 4C are respectively SEM analysis results of the humidity-conditioning ceramics at different sintering temperatures according to an embodiment of the present invention.

第4D圖分別為本發明比較例之調濕陶瓷在850℃燒結的SEM分析結果。 Fig. 4D is a SEM analysis result of sintering of the humidity-conditioning ceramic of Comparative Example of the present invention at 850 ° C, respectively.

第5圖為本發明實施例之調濕陶瓷以不同燒結氣氛之進行燒結的吸放濕曲線。 Fig. 5 is a graph showing the absorption and desorption of the humidity-regulating ceramics in different sintering atmospheres according to an embodiment of the present invention.

第6圖為本發明實施例之調濕陶瓷以不同燒結氣氛在750℃燒結之重金屬固相穩定率。 Figure 6 is a graph showing the solid phase solidification rate of heavy metals sintered at 750 °C in different sintering atmospheres according to an embodiment of the present invention.

以下在實施方式中詳細敘述本發明的詳細特徵以及優點,其 內容足以使任何熟習相關技術者了解本發明的技術內容並據以實施,且根據本說明書所揭露的內容、申請專利範圍及圖式,任何熟悉相關技術者可輕易地理解本發明相關的目的及優點。以下的實施例係進一步詳細說明本發明的觀點,但非以任何觀點限制本發明的範疇。 The detailed features and advantages of the present invention are described in detail below in the embodiments. The content is sufficient for any skilled person to understand the technical content of the present invention and to implement the same, and according to the content, the patent scope and the drawings disclosed in the specification, the relevant objects of the present invention can be easily understood by those skilled in the art and advantage. The following examples are intended to describe the present invention in further detail, but do not limit the scope of the invention in any way.

請參閱第1圖及第2圖,第1圖為本發明一實施例所製備之調濕陶瓷的製作方法之流程圖,第2圖為第1圖之前處理步驟之詳細流程圖。 Please refer to FIG. 1 and FIG. 2 . FIG. 1 is a flow chart of a method for fabricating a humidity-conditioning ceramic prepared according to an embodiment of the present invention, and FIG. 2 is a detailed flowchart of a processing step before the first embodiment.

首先,進行一前處理步驟(A)。詳細來說,前處理步驟(A)包含以下三步驟。 First, a pre-processing step (A) is performed. In detail, the pre-processing step (A) comprises the following three steps.

在前處理步驟(A)中,可進一步區分三步驟(如第2圖所示)。在本實施例中,首先蒐集焚化鍋爐灰,將焚化鍋爐灰進行水萃處理,水萃處理後之焚化鍋爐灰經固液分離以形成一焚化鍋爐灰(A1)。在本實施例中,首先執行水萃的前處理,藉以去除對重金屬穩定及燒結體耐久性不利的鹽類。詳細來說,在執行水萃時液體與固體比例例如為5:1,萃取時間例如為5分鐘,次數例如為2次。待水萃完成後,將焚化鍋爐灰固液分離。 In the pre-processing step (A), the three steps can be further distinguished (as shown in Fig. 2). In the present embodiment, the incineration boiler ash is first collected, the incineration boiler ash is subjected to water extraction treatment, and the incineration boiler ash after the water extraction treatment is separated by solid-liquid separation to form an incineration boiler ash (A1). In the present embodiment, the pretreatment of the water extraction is first performed to remove salts which are detrimental to the stability of the heavy metal and the durability of the sintered body. In detail, the ratio of the liquid to the solid at the time of performing the water extraction is, for example, 5:1, the extraction time is, for example, 5 minutes, and the number of times is, for example, 2 times. After the water extraction is completed, the incinerator boiler ash solid liquid is separated.

其中,焚化鍋爐灰是指經由焚化爐燃燒處理後所獲得的鍋爐灰。焚化鍋爐灰例如包含有22.25wt%的鈣、6.23wt%的矽、2.55wt%的鋁、1.91wt%的鐵、1.76wt%的鎂、3.71wt%的鈉、3.91wt%的鉀、微量之鉛、鋅、鎘、銅、鉻(以助熔劑在高溫將焚化鍋爐灰熔解為液體後進行元素分析的量測結果)。一般而言,由於焚化鍋爐灰還含有重金屬,因而屬於有害廢棄物。因此,焚化鍋爐灰在使用上需要滿足諸多限制,例如這些重金屬的溶出試驗結果應遵守相關規定。需注意的是,上述焚化鍋爐灰的元素組成僅是用以舉例說明,並非用以限定本發明。 Among them, the incineration boiler ash refers to the boiler ash obtained after the combustion treatment by the incinerator. The incineration boiler ash includes, for example, 22.25 wt% of calcium, 6.23 wt% of rhodium, 2.55 wt% of aluminum, 1.91 wt% of iron, 1.76 wt% of magnesium, 3.71 wt% of sodium, 3.91 wt% of potassium, and trace amounts of Lead, zinc, cadmium, copper, chromium (measurement results of elemental analysis after melting the incineration boiler ash into a liquid at a high temperature). In general, incineration boiler ash is also a hazardous waste because it also contains heavy metals. Therefore, the incineration boiler ash needs to meet many restrictions in its use. For example, the dissolution test results of these heavy metals should comply with relevant regulations. It should be noted that the elemental composition of the incineration boiler ash described above is for illustrative purposes only and is not intended to limit the invention.

進行一廢棄玻璃回收程序,以提供一廢棄玻璃(A2)。在本實施例中,是使用棕色玻璃瓶,收集後去除標籤、清洗、烘乾,然後進行破碎,再以顎碎機將玻璃破碎成更小的細粉,最後以200號篩選備用。 A waste glass recycling procedure is performed to provide a waste glass (A2). In this embodiment, a brown glass bottle is used, and after collecting, the label is removed, washed, dried, and then crushed, and then the glass is broken into smaller fine powder by a masher, and finally filtered by 200.

其中,廢棄玻璃例如包含有4.79wt%的鈣、22.10wt%的矽、1.03wt%的鋁、0.20wt%的鐵、0.62wt%的鎂、6.58wt%的鈉、0.41wt%的鉀、微量之鉛、銅、鉻(以助熔劑在高溫將廢棄玻璃熔解為液體後進行元素分析的量測結果)。需注意的是,上述廢棄玻璃的元素組成僅是用以舉例說明,並非用以限定本發明。 Wherein, the waste glass contains, for example, 4.79 wt% of calcium, 22.10 wt% of rhodium, 1.03 wt% of aluminum, 0.20 wt% of iron, 0.62 wt% of magnesium, 6.58 wt% of sodium, 0.41 wt% of potassium, and trace amount. Lead, copper, and chromium (measurement results of elemental analysis after the flux is melted into a liquid at a high temperature). It should be noted that the elemental composition of the above waste glass is for illustrative purposes only and is not intended to limit the invention.

提供一坡縷石(A3)。在本實施例中,是使用採用工業級之坡縷石。 Provide a rock (A3). In the present embodiment, the use of industrial grade palygorskite is used.

詳細來說,坡縷石是屬於海泡石族的一種礦石。坡縷石是由蒙脫石轉化而成。坡縷石是由含水的層鏈狀鎂質矽酸鹽組成,亦即坡縷石是屬於鎂質矽酸鹽礦物。坡縷石的組成例如包含1.19wt%的鈣、12.48wt%的矽、2.6wt%的鋁、1.15wt%的鐵、3.13wt%的鎂、0.24wt%的鈉、1.01wt%的鉀(以助熔劑在高溫將坡縷石熔解為液體後進行元素分析的量測結果)。需注意的是,上述坡縷石的元素組成僅是用以舉例說明,並非用以限定本發明。 In detail, palygorskite is an ore belonging to the sepiolite family. Palygorskite is converted from montmorillonite. The palygorskite is composed of an aqueous layered magnesium silicate, that is, the palygorskite belongs to the magnesia silicate mineral. The composition of palygorskite comprises, for example, 1.19 wt% calcium, 12.48 wt% rhodium, 2.6 wt% aluminum, 1.15 wt% iron, 3.13 wt% magnesium, 0.24 wt% sodium, 1.01 wt% potassium ( The measurement result of the elemental analysis after the flux melts the palygorskite into a liquid at a high temperature. It should be noted that the elemental composition of the palygorskite described above is for illustrative purposes only and is not intended to limit the invention.

需注意的是,上述步驟(A1)、(A2)、(A3)之順序並非用以限定本發明,使用者可根據其需求來選擇步驟(A1)、(A2)、(A3)適當之順序。舉例來說,使用者可以先執行步驟(A3),再依序執行步驟(A1)及(A2)。 It should be noted that the order of the above steps (A1), (A2), and (A3) is not intended to limit the present invention, and the user may select the appropriate order of steps (A1), (A2), and (A3) according to their needs. . For example, the user may perform step (A3) first, and then perform steps (A1) and (A2) in sequence.

在執行前處理步驟(A)之後,將焚化鍋爐灰、廢棄玻璃及坡縷石混合以製成一生胚(B)。 After the pre-treatment step (A), the incineration boiler ash, the waste glass, and the palygorskite are mixed to form a green embryo (B).

在本發明實施例中,焚化鍋爐灰的用量為5-60wt%,廢棄玻 璃的用量為10-85wt%,坡縷石的用量為10-60wt%,藉此,所製備的調濕陶瓷具有較佳的調濕效果。 In the embodiment of the present invention, the amount of the incinerator boiler ash is 5 to 60 wt%, and the waste glass is discarded. The amount of the glass is from 10 to 85% by weight, and the amount of the palygorskite is from 10 to 60% by weight, whereby the prepared humidity-conditioning ceramic has a better humidity control effect.

在本發明部分實施例中,焚化鍋爐灰的用量為10-30wt%,廢棄玻璃的用量為50-80wt%,坡縷石的用量為10-30wt%。在本發明部分實施例中,焚化鍋爐灰的用量為10-20wt%,廢棄玻璃的用量為60-75wt%,坡縷石的用量為15-25wt%。 In some embodiments of the present invention, the incineration boiler ash is used in an amount of 10 to 30% by weight, the waste glass is used in an amount of 50 to 80% by weight, and the palygorskite is used in an amount of 10 to 30% by weight. In some embodiments of the present invention, the amount of incineration boiler ash is 10-20 wt%, the amount of waste glass is 60-75 wt%, and the amount of palygorskite is 15-25 wt%.

使用者可根據其需求來選擇焚化鍋爐灰、廢棄玻璃、坡縷石適當的重量比例。舉例來說,焚化鍋爐灰的用量例如為5wt%、10wt%、15wt%、20wt%、25wt%、30wt%、35wt%、40wt%、45wt%、50wt%、55wt%、60wt%;廢棄玻璃的用量例如為10wt%、15wt%、20wt%、25wt%、30wt%、35wt%、40wt%、45wt%、50wt%、55wt%、60wt%、65wt%、70wt%、75wt%、80wt%;坡縷石的用量為例如為10wt%、15wt%、20wt%、25wt%、30wt%、35wt%、40wt%、45wt%、50wt%、55wt%、60wt%,藉以提升調濕陶瓷的調濕效果。在本實施例及部分其他實施例中,焚化鍋爐灰的用量為10wt%,廢棄玻璃的用量為70wt%,坡縷石的用量為20wt%,藉此,所製備的調濕陶瓷具有更佳調濕效果。 Users can choose the appropriate weight ratio of incineration boiler ash, waste glass, and palygorskite according to their needs. For example, the amount of incineration boiler ash is, for example, 5 wt%, 10 wt%, 15 wt%, 20 wt%, 25 wt%, 30 wt%, 35 wt%, 40 wt%, 45 wt%, 50 wt%, 55 wt%, 60 wt%; The amount is, for example, 10 wt%, 15 wt%, 20 wt%, 25 wt%, 30 wt%, 35 wt%, 40 wt%, 45 wt%, 50 wt%, 55 wt%, 60 wt%, 65 wt%, 70 wt%, 75 wt%, 80 wt%; The amount of stone used is, for example, 10 wt%, 15 wt%, 20 wt%, 25 wt%, 30 wt%, 35 wt%, 40 wt%, 45 wt%, 50 wt%, 55 wt%, 60 wt%, thereby improving the humidity control effect of the humidity control ceramic. In this embodiment and some other embodiments, the amount of the incinerator boiler ash is 10% by weight, the amount of waste glass is 70% by weight, and the amount of palygorskite is 20% by weight, whereby the prepared humidity-conditioning ceramic has better adjustment. Wet effect.

在本實施例及部分其他實施例中,生胚是以2000psi之壓力壓製成型,且壓製時間為1分鐘。待壓製成型後,再放入105℃烘箱中烘乾24小時,以確保生坯形狀完整性。 In this and some other embodiments, the green embryos were compression molded at a pressure of 2000 psi and the pressing time was 1 minute. After being pressed and molded, it was placed in an oven at 105 ° C for 24 hours to ensure the shape integrity of the green body.

在本實施例中,所製成之生坯尺寸大小為:長10公分、寬5公分及厚0.5公分。 In this embodiment, the green size produced is: 10 cm in length, 5 cm in width, and 0.5 cm in thickness.

需注意的是,在上述步驟(B)中,生坯的含水率為 10~20wt%,含水率是以生胚之總重量為基準。若含水率過高將導致坯體無法成型,而如果含水率過低則會造成坯體破裂。 It should be noted that in the above step (B), the moisture content of the green body 10~20wt%, the water content is based on the total weight of the raw embryo. If the moisture content is too high, the green body will not be formed, and if the moisture content is too low, the green body will be broken.

在本實施例及部分其他實施例中,生坯的含水率為15wt%。藉此,以達到較佳的成型效果。 In this and some other embodiments, the green body has a moisture content of 15% by weight. Thereby, a better molding effect is achieved.

最後,將生胚執行一燒結程序(C)。藉此,以燒結形成調濕陶瓷。在本發明實施例中,燒結程序之燒結溫度為700~1000℃。在本實施例及部分其他實施例中,燒結程序之燒結溫度為700~800℃。在本實施例及部分其他實施例中,燒結程序之燒結溫度為750℃。使用者可以根據其調濕陶瓷的需求來選擇合適的燒結溫度。詳細來說,使用者可過調整燒結溫度來改變所製備的調濕陶瓷的調濕能力及機械強度。當燒結溫度越低時,所製備的調濕陶瓷具有較佳的調濕能力,而當燒結溫度越高時,所製備的調濕陶瓷則具有較佳的機械強度。其中,燒結程序之升溫速率介於1~30℃/min。待溫度到達750℃時,持溫20分鐘後自然降至室溫。其中,燒結程序可以是氧化燒結(高溫矩形爐,空氣氣氛燒結,有氧環境)、還原燒結(管狀爐,氮氣氣氛燒結,無氧環境)。藉此,所燒結製成的調濕陶瓷同時具有優異的調濕能力以及機械強度。 Finally, the firing process is performed on the green embryo (C). Thereby, the humidity-conditioning ceramic is formed by sintering. In the embodiment of the invention, the sintering temperature of the sintering process is 700 to 1000 °C. In this embodiment and some other embodiments, the sintering temperature of the sintering process is 700 to 800 °C. In this and some other embodiments, the sintering temperature of the sintering procedure was 750 °C. The user can select the appropriate sintering temperature according to the requirements of the humidity-conditioning ceramic. In detail, the user can adjust the sintering temperature to change the humidity control ability and mechanical strength of the prepared humidity control ceramic. When the sintering temperature is lower, the prepared humidity-conditioning ceramic has better humidity control ability, and when the sintering temperature is higher, the prepared humidity-conditioning ceramic has better mechanical strength. Among them, the heating rate of the sintering process is between 1 and 30 ° C / min. When the temperature reached 750 ° C, it was naturally cooled to room temperature after holding for 20 minutes. Among them, the sintering process may be oxidative sintering (high temperature rectangular furnace, air atmosphere sintering, aerobic environment), reduction sintering (tubular furnace, nitrogen atmosphere sintering, oxygen-free environment). Thereby, the humidity-tuned ceramic produced by sintering has both excellent humidity control ability and mechanical strength.

在本發明實施例中,調濕陶瓷的焚化鍋爐灰的用量為5-60wt%,廢棄玻璃的用量為10-85wt%坡縷石的用量為10-60wt%。在本發明部分實施例中,焚化鍋爐灰的用量為10-30wt%,廢棄玻璃的用量為50-80wt%,坡縷石的用量為10-30wt%。在本發明部分實施例中,焚化鍋爐灰的用量為10-20wt%,廢棄玻璃的用量為60-75wt%,坡縷石的用量為15-25wt%。使用者可根據其需求來選擇焚化鍋爐灰、廢棄玻璃、坡縷石的 重量比例,於此不重複描述。 In the embodiment of the present invention, the amount of the incineration boiler ash of the humidity-control ceramic is 5 to 60 wt%, and the amount of the waste glass is 10 to 85 wt%, and the amount of the palygorskite is 10 to 60 wt%. In some embodiments of the present invention, the incineration boiler ash is used in an amount of 10 to 30% by weight, the waste glass is used in an amount of 50 to 80% by weight, and the palygorskite is used in an amount of 10 to 30% by weight. In some embodiments of the present invention, the amount of incineration boiler ash is 10-20 wt%, the amount of waste glass is 60-75 wt%, and the amount of palygorskite is 15-25 wt%. Users can choose incineration boiler ash, waste glass, palygorskite according to their needs. The weight ratio is not repeated here.

如上所述,由於本案所使用的焚化鍋爐灰具發泡特性以及多孔特性,並且透過廢棄玻璃作為膠結劑,因而可在維持調濕陶瓷的機械強度下成功製備具有較佳調濕效果的調濕陶瓷。 As described above, since the incineration boiler used in the present case has foaming characteristics and porous characteristics, and through the waste glass as a cementing agent, it is possible to successfully prepare a humidity control having a better humidity control effect while maintaining the mechanical strength of the humidity control ceramic. ceramics.

以下測試本發明實施例之調濕陶瓷。 The humidity-conditioning ceramics of the examples of the present invention were tested as follows.

一、調濕性能評價基準 First, the humidity conditioning performance evaluation benchmark

在本發明中,吸放濕試驗方法是以JIS A 1470-1進行測試,並且依照日本所定之調濕建材調濕性能評價基準(調湿建材性能評価委員会,2006),中濕域(50~70%)的吸放濕試驗,24小時連續試驗中,依前12小時的吸濕量而評定為不同等級,且後12小時的放濕量需為吸濕量的70%以上,才符合日本的調濕材料的評價基準。 In the present invention, the moisture absorption and desorption test method is tested in accordance with JIS A 1470-1, and in accordance with Japan's moisture conditioning performance evaluation benchmark for building materials (Guidelines for Conditioning Building Materials Evaluation, 2006), medium wet field (50) ~70%) The moisture absorption and desorption test, in the 24-hour continuous test, is rated as different grade according to the first 12 hours of moisture absorption, and the amount of moisture removal after the last 12 hours needs to be more than 70% of the moisture absorption. The evaluation criteria for Japanese humidity control materials.

請參閱第3圖,第3圖為本發明實施例之調濕陶瓷在不同燒結溫度的吸放濕試驗。如圖所示,本發明實施例之調濕陶瓷的放濕量皆符合評價基準之要求(吸濕量的70%以上),其吸濕量分別為85.22g/m2、65.26g/m2、42.38g/m2、23.16g/m2,由圖顯示在700℃的吸濕量最多,可達到最高級(第三級)之標準。另請參閱第4A圖至第4D圖,第4A圖至第4C圖分別為本發明實施例之調濕陶瓷在不同燒結溫度的SEM分析結果,第4D圖分別為本發明比較例之調濕陶瓷在850℃燒結的SEM分析結果。如第4A圖所示,在700℃下由於燒結溫度較低,顆粒的排列也較為鬆散,形成較多開放孔隙,使吸濕效果較佳。如第4B圖所示,在750℃下部分玻璃開始熔融使顆粒開始黏結導致部分孔洞開始縮減,因而調濕量稍微降低,但仍可達第二級調濕材料。如第4C圖所示,在800℃下玻璃產生熔融狀態,燒結體內開放 孔隙開始被填滿,部分轉為封閉孔洞。如第4D圖所示,在850℃下由於提高燒結溫度致使廢棄玻璃有較長的時間形成熔融態形成緻密化,進而封閉孔洞結構導致水蒸氣吸附性能消失,所製備之調濕陶瓷的吸濕量下降。 Please refer to FIG. 3, which is a moisture absorption and desorption test of the humidity-conditioning ceramics at different sintering temperatures according to an embodiment of the present invention. As shown, the amount of moisture release are in compliance with the requirements of the evaluation criteria (moisture content of 70% or more) of the humidity-ceramic according to embodiments of the present invention, the amount of moisture absorption were 85.22g / m 2, 65.26g / m 2 , 42.38g / m 2, 23.16g / m 2, the graph shows the amount of moisture up to 700 deg.] C, up to the highest level (third level) of the standard. Please refer to FIG. 4A to FIG. 4D , and FIG. 4A to FIG. 4C are respectively SEM analysis results of the humidity-control ceramics at different sintering temperatures according to an embodiment of the present invention, and FIG. 4D is a humidity-conditioning ceramic of a comparative example of the present invention, respectively. SEM analysis results of sintering at 850 °C. As shown in Fig. 4A, at 700 ° C, the sintering temperature is lower, the arrangement of the particles is looser, and more open pores are formed, so that the moisture absorption effect is better. As shown in Fig. 4B, at 750 ° C, part of the glass begins to melt to cause the particles to begin to bond, causing some of the pores to begin to shrink, so that the amount of humidity control is slightly lowered, but still reaches the second-stage humidity-conditioning material. As shown in Fig. 4C, at 800 ° C, the glass is in a molten state, and the open pores in the sintered body are initially filled and partially turned into closed pores. As shown in Fig. 4D, at 850 ° C, the sintering temperature is increased, so that the waste glass has a long time to form a molten state to form a densification, thereby blocking the pore structure and causing the water vapor adsorption property to disappear, and the moisture permeability of the prepared humidity control ceramic is eliminated. The amount drops.

二、機械特性 Second, mechanical characteristics

請參閱下表一。表一為本發明實施例及比較例之調濕陶瓷以氧化燒結之燒結體機械特性。如表一所示,燒結溫度與收縮率、抗彎強度成正比,與視孔隙率、吸水率成反比。其中,視孔隙率與吸水率與調濕能力有所關連,可作為調濕能力,尤其是吸濕能力的初步指標。 Please refer to the table below. Table 1 shows the mechanical properties of the sintered body of the humidity-control ceramics of the examples and comparative examples of the present invention. As shown in Table 1, the sintering temperature is proportional to the shrinkage rate and the flexural strength, and inversely proportional to the apparent porosity and water absorption. Among them, the apparent porosity and water absorption are related to the humidity control ability, and can be used as a preliminary indicator of the humidity control ability, especially the moisture absorption capacity.

如表一所示,700℃之調濕陶瓷的調濕能力雖然最好,但平均抗彎強度較低;750℃之調濕陶瓷的平均抗彎強度已達6.12MPa,並且可符合CNS3299-4陶瓷面磚強度要求,並且調濕能力為評價基準的第二級;800℃之調濕陶瓷的抗彎強度可符合CNS要求,並且可維持調濕能力於第一級之評價基準。 As shown in Table 1, the humidity control ability of 700 °C humidity control ceramics is the best, but the average bending strength is low; the average bending strength of 750 °C humidity control ceramics has reached 6.12 MPa, and can meet CNS3299-4 Ceramic tile strength requirements, and humidity control capacity is the second level of evaluation benchmark; 800 ° C humidity control ceramics bending strength can meet the CNS requirements, and can maintain the humidity control capacity in the first level of evaluation criteria.

三、氧化與還原燒結之比較 Third, the comparison of oxidation and reduction sintering

在本發明中,分別以矩形爐及管狀爐在空氣氣氛之氧化燒結及氮氣氣氛之還原燒結的,並分析二者之調濕能力、機械特性(抗彎強度)、燒結過程重金屬揮發及燒結體重金屬穩定性。 In the present invention, the rectangular furnace and the tubular furnace are respectively oxidized and sintered in an air atmosphere and reduced and sintered in a nitrogen atmosphere, and the humidity control ability, mechanical properties (bending strength), and heavy metal volatilization and sintered body in the sintering process are analyzed. Heavy metal stability.

請參閱第5圖,第5圖為本發明實施例之調濕陶瓷以不同燒結氣氛之進行燒結的吸放濕曲線(燒結溫度750℃)。如第5圖所示,二種燒結氣氛對所製成之調濕陶瓷的調濕能力相近,均符合日本評價基準的第二級要求。 Referring to FIG. 5, FIG. 5 is a moisture absorption and desorption curve (sintering temperature of 750 ° C) of the humidity-conditioning ceramics sintered in different sintering atmospheres according to an embodiment of the present invention. As shown in Fig. 5, the two sintering atmospheres have similar humidity control capabilities to the prepared humidity-conditioning ceramics, and all meet the second-level requirements of the Japanese evaluation standard.

請一併參閱表二,表二本發明實施例之調濕陶瓷以不同燒結氣氛進行燒結的機械特性。 Please refer to Table 2 and Table 2 for the mechanical properties of the humidity-conditioning ceramics of the embodiment of the present invention sintered in different sintering atmospheres.

如表二所示,二種燒結氣氛對所製成之調濕陶瓷的體密度、收縮率、視孔隙率及吸水率等機械特性影響相近;其中以氮氣燒結之調濕陶瓷具有較佳的抗彎強度,其抗彎強度已明確高出CNS3299-4陶瓷面磚強度要求。 As shown in Table 2, the two sintering atmospheres have similar effects on the mechanical properties such as bulk density, shrinkage ratio, apparent porosity and water absorption of the prepared humidity-control ceramics; among them, the humidity-regulating ceramics sintered with nitrogen have better resistance. Bending strength, its bending strength has been clearly higher than the CNS3299-4 ceramic tile strength requirements.

如第5圖及表二所示,二種燒結氣氛對所製成之調濕陶瓷的調濕能力及機械特性都相近。 As shown in Fig. 5 and Table 2, the two sintering atmospheres have similar humidity control capabilities and mechanical properties to the prepared humidity control ceramics.

四、重金屬溶出量 Fourth, heavy metal dissolution

以下測試本發明實施例之調濕陶瓷的重金屬溶出量。請參閱表三,表三為本發明實施例之調濕陶瓷以不同燒結氣氛在750℃燒結毒性溶出試驗結果。 The amount of heavy metal eluted from the humidity-conditioning ceramics of the examples of the present invention was tested below. Please refer to Table 3, Table 3 for the results of the toxic dissolution test of the humidity-control ceramics at 750 ° C in different sintering atmospheres according to the embodiment of the present invention.

如表三所示,Pb、Zn、Cu、Cd溶出濃度皆遠低於再利用標準,亦即本發明之調濕陶瓷的重金屬在環境中非常不易溶出。另一方面,重金屬Cr的溶出濃度低於再利用標準,為穩定安全的環保產品,若使用氮氣氣氛燒結可進一步將重金屬Cr溶出值減少至十分之一以下。因此,本發明可有效控制燒結過程中重金屬的溶出量,並且使用氮氣氣氛之還原燒結,可進一步提升所製備之調濕陶瓷的環保性能。 As shown in Table 3, the dissolution concentrations of Pb, Zn, Cu, and Cd are far lower than the reuse standards, that is, the heavy metals of the humidity-conditioning ceramics of the present invention are very difficult to dissolve in the environment. On the other hand, the dissolution concentration of the heavy metal Cr is lower than the recycling standard, and is a stable and safe environmentally friendly product. If the sintering is performed using a nitrogen atmosphere, the elution value of the heavy metal Cr can be further reduced to less than one tenth. Therefore, the present invention can effectively control the elution amount of heavy metals in the sintering process, and the reduction and sintering in a nitrogen atmosphere can further improve the environmental performance of the prepared humidity-conditioning ceramics.

五、重金屬固相穩定率 Five, heavy metal solid phase stability rate

以下測試本發明實施例之調濕陶瓷的重金屬固相穩定率。請參閱第6圖,第6圖為本發明實施例之調濕陶瓷以不同燒結氣氛在750℃燒結之重金屬固相穩定率。 The heavy metal solid phase stability of the humidity-conditioning ceramics of the examples of the present invention was tested as follows. Please refer to FIG. 6. FIG. 6 is a solid phase solidification rate of heavy metals sintered at 750 ° C in different sintering atmospheres according to an embodiment of the present invention.

如第6圖,重金屬Pb在二種燒結氣氛下都有75%留在固相,並且Zn、Cu、Cr在二種燒結氣氛下大於75%留在固相。因此,本發明可有效控制重金屬於燒結過程中揮發所造成的二次汙染。 As shown in Fig. 6, the heavy metal Pb remains 75% in the solid phase in both sintering atmospheres, and Zn, Cu, and Cr remain in the solid phase in more than 75% under the two sintering atmospheres. Therefore, the present invention can effectively control secondary pollution caused by volatilization of heavy metals during sintering.

根據上述本發明所揭露之實施例,由於本發明是利用焚化鍋爐灰、廢棄玻璃及坡縷石製成調濕陶瓷,因而可以達成以下技術功效: According to the embodiment of the invention disclosed above, since the invention utilizes incineration boiler ash, waste glass and palygorskite to make a humidity-conditioning ceramic, the following technical effects can be achieved:

(1)本案利用焚化鍋爐灰、廢棄玻璃及坡縷石製備具有高調濕效果的陶瓷材料,並且陶瓷材料具有足夠的機械強度而可供使用,因而本案可有效解決焚化鍋爐灰以及廢棄玻璃處置的問題,進而達到材料有效的再利用,具有環保、高經濟價值等多重功效。 (1) In this case, the ceramic material with high humidity control effect is prepared by using incinerator boiler ash, waste glass and palygorskite, and the ceramic material has sufficient mechanical strength to be used, so the case can effectively solve the disposal of incinerator boiler ash and waste glass. The problem, in turn, achieves effective reuse of materials, and has multiple functions such as environmental protection and high economic value.

(2)本案利用焚化鍋爐灰及廢棄玻璃二廢棄物製備調濕陶 瓷,藉此,在商業實施上具有相當大的成本優勢。 (2) In this case, the incineration boiler ash and waste glass waste were used to prepare the humidity control pottery. Porcelain, by virtue of this, has considerable cost advantages in commercial implementation.

(3)本案調濕陶瓷最高可在12小時達200g/m2吸濕量,已遠超過日本的調濕建材評價基準最高級(71g/m2)之規定,是具有優異調濕能力的調濕陶瓷。同時,本案由於具有適當的焚化鍋爐灰、廢棄玻璃及坡縷石重量比例,因而在750℃即可燒製吸濕量65.26g/m2,放濕率75.32%之燒結體,達到日本評價基準第二級之規定,且機械強度通過陶瓷面磚強度之要求(6.12MPa)。 (3) The humidity-control ceramics in this case can reach a maximum moisture absorption of 200g/m 2 in 12 hours, which far exceeds the highest level (71g/m 2 ) of Japan's humidity-control building materials evaluation benchmark. Wet ceramics. At the same time, in this case, due to the appropriate proportion of incineration boiler ash, waste glass and palygorskite, the sintered body with a moisture absorption of 65.26g/m 2 and a moisture release rate of 75.32% can be fired at 750 °C, which meets the Japanese evaluation criteria. The second level is specified, and the mechanical strength is determined by the strength of the ceramic tile (6.12 MPa).

(4)本案適當的材料組成以及燒結溫度,可有效確保重金屬停留於所製成之調濕陶瓷內,因而所製成之調濕陶瓷內在環境中為相當穩定安全。 (4) The proper material composition and sintering temperature of the case can effectively ensure that the heavy metal stays in the prepared humidity-regulating ceramic, so that the prepared humidity-regulating ceramic is quite stable and safe in the internal environment.

雖然本發明之實施例揭露如上所述,然並非用以限定本發明,任何熟習相關技術者,在不脫離本發明之精神和範圍內,舉凡依本發明申請範圍所述之形狀、構造、特徵及精神當可做些許之變更,因此本發明之專利保護範圍須視本說明書所附之申請專利範圍所界定者為準。 Although the embodiments of the present invention are disclosed above, it is not intended to limit the present invention, and those skilled in the art can devise shapes, structures, and features according to the scope of the present application without departing from the spirit and scope of the present invention. And the spirit of the invention is subject to change. Therefore, the scope of patent protection of the present invention is subject to the scope of the patent application attached to the specification.

Claims (8)

一種調濕陶瓷,其係按照下列比例加以混合燒結製成:一焚化鍋爐灰,該焚化鍋爐灰的用量為5-60wt%;一廢棄玻璃,該廢棄玻璃的用量為10-85wt%;以及一坡縷石,該坡縷石的用量為10-60wt%。 A humidity-controlling ceramic prepared by mixing and sintering according to the following ratio: an incineration boiler ash, the incineration boiler ash is used in an amount of 5 to 60% by weight; and a waste glass is used in an amount of 10 to 85% by weight; and The palygorskite is used in an amount of 10 to 60% by weight. 如請求項1所述之調濕陶瓷,其中該焚化鍋爐灰的用量為10wt%,該廢棄玻璃的用量為70wt%,該坡縷石的用量為20wt%。 The humidity-conditioning ceramic according to claim 1, wherein the incineration boiler ash is used in an amount of 10% by weight, the waste glass is used in an amount of 70% by weight, and the palygorskite is used in an amount of 20% by weight. 一種調濕陶瓷的製作方法,包含:進行一前處理步驟,包含:蒐集焚化鍋爐灰,將該焚化鍋爐灰進行水萃處理,水萃處理後之該焚化鍋爐灰經一固液分離、過濾烘乾、冷卻、破碎之處理,以形成一焚化鍋爐灰;進行一廢棄玻璃回收程序,以提供一廢棄玻璃;以及提供一坡縷石;將該焚化鍋爐灰、該廢棄玻璃及該坡縷石混合以製成一生胚,其中,焚化鍋爐灰的用量為5-60wt%,廢棄玻璃的用量為10-85wt%坡縷石的用量為10-60wt%;以及將該生胚執行一燒結程序,該燒結程序之燒結溫度為700℃~1000℃。 The invention relates to a method for preparing a humidity-controlling ceramic, comprising: performing a pre-treatment step, comprising: collecting incineration boiler ash, performing water extraction treatment on the incinerator boiler ash, and separating the incineration boiler ash by a solid-liquid separation, filtering and drying after the water extraction treatment Drying, cooling, and crushing treatment to form an incineration boiler ash; performing a waste glass recovery procedure to provide a waste glass; and providing a palygorskite; mixing the incineration boiler ash, the waste glass, and the palygorskite To produce a raw embryo, wherein the amount of the incinerator boiler ash is 5 to 60 wt%, the amount of the waste glass is 10 to 85 wt%, and the amount of the palygorskite is 10 to 60 wt%; and the raw embryo is subjected to a sintering process, The sintering temperature of the sintering process is 700 ° C to 1000 ° C. 如請求項3所述之調濕陶瓷的製作方法,其中該焚化鍋爐灰的用量為10wt%,該廢棄玻璃的用量為70wt%,該坡縷石的用量為20wt%。 The method for producing a humidity-controlling ceramic according to claim 3, wherein the incineration boiler ash is used in an amount of 10% by weight, the waste glass is used in an amount of 70% by weight, and the palygorskite is used in an amount of 20% by weight. 如請求項3所述之調濕陶瓷的製作方法,其中於該製成一生胚之步驟中, 該生坯的含水率為10~20wt%,該生坯的含水率是以該生胚之總重量為基準。 The method for producing a humidity-controlling ceramic according to claim 3, wherein in the step of preparing a raw embryo, The green body has a water content of 10 to 20% by weight, and the moisture content of the green body is based on the total weight of the green embryo. 如請求項3所述之調濕陶瓷的製作方法,其中於該製成一生胚之步驟中,該生坯的含水率為15wt%,該生坯的含水率是以該生胚之總重量為基準。 The method for preparing a humidity-controlling ceramic according to claim 3, wherein in the step of forming a green embryo, the green matter has a water content of 15% by weight, and the moisture content of the green body is the total weight of the green embryo. Benchmark. 如請求項3所述之調濕陶瓷的製作方法,其中於該製成一生胚之步驟中,該生胚是以2000psi之壓力壓製成型,且壓製時間為1分鐘。 The method for producing a humidity-conditioning ceramic according to claim 3, wherein in the step of forming a green embryo, the green embryo is press-molded at a pressure of 2000 psi, and the pressing time is 1 minute. 如請求項3所述之調濕陶瓷的製作方法,其中該燒結程序之升溫速率介於1~30℃/min。 The method for preparing a humidity-conditioning ceramic according to claim 3, wherein the sintering process has a heating rate of 1 to 30 ° C/min.
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