TWI729963B - Composite adsorbent, method of preparing the same and use thereof - Google Patents

Composite adsorbent, method of preparing the same and use thereof Download PDF

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TWI729963B
TWI729963B TW109141445A TW109141445A TWI729963B TW I729963 B TWI729963 B TW I729963B TW 109141445 A TW109141445 A TW 109141445A TW 109141445 A TW109141445 A TW 109141445A TW I729963 B TWI729963 B TW I729963B
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zeolite
adsorbent
microwave
composite
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TW202220751A (en
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林淵淙
馮奕淞
周豐志
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國立中山大學
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Abstract

A composite adsorbent, a method of preparing the same, and a use thereof are provided. The method includes the steps of: providing a silica raw material and an aluminum slag powder; adding the silica raw material and the aluminum slag powder into a sodium hydroxide solution and mixing, and then performing a microwave-assisted hydrothermal synthesis reaction to obtain a zeolite; and immersing the zeolite and titanium isopropoxide in an ethanol solution and mixing, then adding deionized water and stirring, and then performing the microwave-assisted hydrothermal synthesis reaction to obtain the composite adsorbent. A ratio of zeolite and titanium dioxide photocatalyst in the composite adsorbent is between 3:7 and 7:3 by weight. The composite adsorbent is used for absorbing an air pollutant, and the air pollutant includes carbon dioxide, carbon monoxide, formaldehyde, acetaldehyde, phenol or ozone.

Description

複合材料吸附劑、其製備方法及其用途Composite material adsorbent, its preparation method and its use

本發明係有關一種吸附劑,尤指一種複合材料;本發明亦有關一種吸附劑之製備方法,尤指一種複合材料吸附劑之製備方法;本發明亦有關一種吸附劑之用途,尤指一種複合材料吸附劑之用途。The present invention relates to an adsorbent, especially a composite material; the present invention also relates to a preparation method of an adsorbent, especially a preparation method of a composite material adsorbent; the present invention also relates to the use of an adsorbent, especially a composite The use of material adsorbents.

研究資料顯示,人們待在室內及交通工具內的時間分別約佔據所有活動時間的89%及6%,而其餘的時間則是於室外活動,顯見,人們大部分的時間是待於室內。室內空氣品質與人體健康之間具有正向關聯,即,長期性暴露於不良的室內空氣品質之環境,將危害人體健康。影響室內空氣品質的主要因子為室內空氣污染物,包括二氧化碳、一氧化碳、甲醛、乙醛、苯酚、總揮發性有機化合物、細菌、真菌、粒徑小於等於十微米之懸浮、微粒(PM10)、粒徑小於或等於2.5微米之懸浮微粒(PM2.5)等。因此,去除室內空氣污染物將有助於避免人體健康受到危害。Research data shows that people spend about 89% and 6% of all activity time indoors and transportation, respectively, while the rest of the time is spent outdoors. Obviously, people spend most of their time indoors. There is a positive correlation between indoor air quality and human health, that is, long-term exposure to an environment with poor indoor air quality will endanger human health. The main factors affecting indoor air quality are indoor air pollutants, including carbon dioxide, carbon monoxide, formaldehyde, acetaldehyde, phenol, total volatile organic compounds, bacteria, fungi, suspended particles with a particle size of less than or equal to ten microns, particulates (PM10), and particulates. Suspended particles (PM2.5) with a diameter less than or equal to 2.5 microns, etc. Therefore, the removal of indoor air pollutants will help avoid harm to human health.

現有技術主要利用多孔材料之吸附劑來吸附包括二氧化碳、一氧化碳、甲醛、乙醛、苯酚等之室內空氣污染物,以去除室內空氣污染物。然而,當該多孔材料之吸附劑達到吸附飽和時,將導致多孔材料之吸附劑的吸附效果降低並失去吸附能力。The prior art mainly uses porous material adsorbents to adsorb indoor air pollutants including carbon dioxide, carbon monoxide, formaldehyde, acetaldehyde, phenol, etc., to remove indoor air pollutants. However, when the adsorbent of the porous material reaches adsorption saturation, the adsorption effect of the adsorbent of the porous material will be reduced and the adsorption capacity will be lost.

此外,在諸如廢玻璃及廢鋁渣之工業廢棄物方面,廢玻璃之處理方式普遍為倒入垃圾掩埋場或鋪設道路,然而,垃圾掩埋場之空間有限且玻璃無法被生物分解,因此未被回收再利用之廢玻璃將造成環境的負擔。另,廢鋁渣倘若未被妥善處理而與水接觸時,容易釋出具有臭味之氨氣,對環境造成危害。因此,基於環境保護之原則,倘若諸如廢玻璃及廢鋁渣之工業廢棄物未被回收再利用,將會對環境造成危害,進而影響人體的健康。In addition, in terms of industrial wastes such as waste glass and waste aluminum slag, waste glass is generally treated by dumping it into landfills or paving roads. However, the space of landfills is limited and the glass cannot be biodegraded, so it is not The recycled waste glass will cause a burden on the environment. In addition, if the waste aluminum slag is not properly treated and comes into contact with water, it is easy to release odorous ammonia gas, which is harmful to the environment. Therefore, based on the principle of environmental protection, if industrial wastes such as waste glass and aluminum slag are not recycled and reused, they will harm the environment and affect human health.

因此,將諸如廢玻璃及廢鋁渣之工業廢棄物進行回收再利用,並製備可持續吸附包括二氧化碳、一氧化碳、甲醛、乙醛及苯酚等之室內空氣污染物的複合材料吸附劑係本領域亟待解決之問題。Therefore, industrial wastes such as waste glass and aluminum slag are recycled and reused, and composite adsorbents that can sustainably absorb indoor air pollutants including carbon dioxide, carbon monoxide, formaldehyde, acetaldehyde, phenol, etc., are urgently needed in this field. Solve the problem.

為解決上述現有技術之問題,本發明之目的在於提供一種複合材料吸附劑之製備方法,透過使用廢玻璃及廢鋁渣分別製備二氧化矽原料及鋁渣粉末,並利用微波輔助水熱合成方法以製得一沸石,再將沸石與異丙醇鈦透過溶膠凝膠法及微波輔助水熱合成方法以製得一複合材料吸附劑。In order to solve the above-mentioned problems in the prior art, the purpose of the present invention is to provide a method for preparing a composite adsorbent by using waste glass and waste aluminum slag to prepare silicon dioxide raw material and aluminum slag powder, respectively, and using a microwave-assisted hydrothermal synthesis method A zeolite is prepared, and then the zeolite and titanium isopropoxide are passed through a sol-gel method and a microwave-assisted hydrothermal synthesis method to prepare a composite material adsorbent.

本發明之另一目的在於提供一種複合材料吸附劑,以該複合材料吸附劑之總重量計,該沸石及該二氧化鈦光觸媒之重量比係介於3:7與7:3之間。Another object of the present invention is to provide a composite material adsorbent. Based on the total weight of the composite material adsorbent, the weight ratio of the zeolite and the titanium dioxide photocatalyst is between 3:7 and 7:3.

本發明之又一目的在於提供一種複合材料吸附劑用於吸附空氣污染物之用途,其中該吸附空氣污染物包括二氧化碳、一氧化碳、甲醛、乙醛、苯酚或其組合。Another object of the present invention is to provide a composite material adsorbent for adsorbing air pollutants, wherein the adsorbed air pollutants include carbon dioxide, carbon monoxide, formaldehyde, acetaldehyde, phenol or a combination thereof.

為了達成上述目的,本發明提供一種複合材料吸附劑之製備方法,包含下述步驟: 提供二氧化矽原料及鋁渣粉末; 將莫耳比範圍為1:1至5:1之該二氧化矽原料與該鋁渣粉末加入1 M至5 M氫氧化鈉溶液中,混合均勻,以得到一混合物;將該混合物置於一密閉式微波消化器內,於90°C至250°C下進行微波輔助水熱合成反應3分鐘至60分鐘後進行真空過濾,以得到一第三固相材料;將該第三固相材料進行乾燥,以得到一沸石;以及 將重量比範圍為1:5至1:10之該沸石與異丙醇鈦浸於乙醇溶液中,並攪拌均勻;之後加入去離子水並攪拌,以得到一白色凝膠狀物質;將該白色凝膠狀物質進行乾燥,以得到一結晶物;將該結晶物置入該密閉式微波消化器內,於90°C至250°C下進行微波輔助水熱合成反應3分鐘至60分鐘,以得到一複合材料吸附劑 In order to achieve the above objective, the present invention provides a method for preparing a composite adsorbent, which includes the following steps: Provide silicon dioxide raw materials and aluminum slag powder; Add the silicon dioxide raw material and the aluminum slag powder with a molar ratio ranging from 1:1 to 5:1 into a 1 M to 5 M sodium hydroxide solution, and mix them uniformly to obtain a mixture; In a closed microwave digester, microwave-assisted hydrothermal synthesis reaction is performed at 90°C to 250°C for 3 minutes to 60 minutes, and then vacuum filtration is performed to obtain a third solid phase material; Drying to obtain a zeolite; and Dip the zeolite and titanium isopropoxide with a weight ratio ranging from 1:5 to 1:10 in an ethanol solution and stir evenly; then add deionized water and stir to obtain a white gelatinous substance; The gelatinous substance is dried to obtain a crystal; the crystal is placed in the closed microwave digester, and the microwave-assisted hydrothermal synthesis reaction is performed at 90°C to 250°C for 3 minutes to 60 minutes to obtain A composite adsorbent

在一具體實施例中,在提供該二氧化矽原料之步驟中,包括步驟: 將一玻璃粉末加入2M至4M HCl溶液中,於50°C至70°C下攪拌後進行真空過濾,以得到一第一固相材料;以及 將該第一固相材料加入3M至5M H 2SO 4溶液中,於50°C至70°C下攪拌後進行真空過濾,再以去離子水沖洗後進行乾燥,以得到該二氧化矽原料。 In a specific embodiment, the step of providing the silicon dioxide raw material includes the following steps: adding a glass powder to a 2M to 4M HCl solution, stirring at 50°C to 70°C, and then performing vacuum filtration to obtain A first solid-phase material; and adding the first solid-phase material to a 3M to 5M H 2 SO 4 solution, stirring at 50°C to 70°C, vacuum filtration, and then rinsing with deionized water and drying , In order to obtain the silicon dioxide raw material.

在一具體實施例中,在提供該鋁渣粉末之步驟中,包括步驟: 將一廢鋁渣加入0.0001M至0.01M H 2SO 4溶液中,於50°C至70°C下攪拌後進行真空過濾,以得到一第二固相材料;以及 以去離子水沖洗該第二固相材料後進行乾燥,以得到該鋁渣粉末。 In a specific embodiment, the step of providing the aluminum slag powder includes the following steps: adding a waste aluminum slag to a 0.0001M to 0.01MH 2 SO 4 solution, stirring at 50°C to 70°C, and vacuuming Filtering to obtain a second solid phase material; and washing the second solid phase material with deionized water and then drying to obtain the aluminum slag powder.

在一具體實施例中,該微波輔助水熱合成反應係在100°C至220°C下進行10分鐘至50分鐘。In a specific embodiment, the microwave-assisted hydrothermal synthesis reaction is performed at 100°C to 220°C for 10 minutes to 50 minutes.

在一具體實施例中,該微波輔助水熱合成反應係在100°C至180°C下進行10分鐘至30分鐘。In a specific embodiment, the microwave-assisted hydrothermal synthesis reaction is performed at 100°C to 180°C for 10 minutes to 30 minutes.

在一具體實施例中,該微波輔助水熱合成反應係在100°C至140°C下進行10分鐘至20分鐘。In a specific embodiment, the microwave-assisted hydrothermal synthesis reaction is performed at 100°C to 140°C for 10 minutes to 20 minutes.

在一具體實施例中,該微波輔助水熱合成反應係在100°C下進行10分鐘。In a specific embodiment, the microwave-assisted hydrothermal synthesis reaction is carried out at 100°C for 10 minutes.

本發明另提供一種複合材料吸附劑之製備方法所製得之複合材料吸附劑,包括沸石及二氧化鈦光觸媒,其中以該複合材料吸附劑之總重量計,該沸石及該二氧化鈦光觸媒之重量比係介於3:7與7:3之間。The present invention also provides a composite material adsorbent prepared by a method for preparing a composite material adsorbent, comprising a zeolite and a titanium dioxide photocatalyst, wherein based on the total weight of the composite material adsorbent, the weight ratio of the zeolite and the titanium dioxide photocatalyst is intermediate Between 3:7 and 7:3.

在一具體實施例中,以該複合材料吸附劑之總重量計,該沸石及該二氧化鈦光觸媒之重量比係4:6、5:5或6:4。In a specific embodiment, based on the total weight of the composite adsorbent, the weight ratio of the zeolite and the titanium dioxide photocatalyst is 4:6, 5:5, or 6:4.

本發明另提供一種複合材料吸附劑用於吸附空氣污染物之用途,其中該吸附空氣污染物包括,但不限於二氧化碳、一氧化碳、甲醛、乙醛、苯酚或其組合。The present invention also provides a composite material adsorbent for adsorbing air pollutants, wherein the adsorbed air pollutants include, but are not limited to, carbon dioxide, carbon monoxide, formaldehyde, acetaldehyde, phenol or a combination thereof.

本發明之複合材料吸附劑之製備方法透過使用廢玻璃及廢鋁渣分別製備二氧化矽原料及鋁渣粉末,可使玻璃及廢鋁渣被回收再利用,進而避免環境受到危害,達到環境保護之目的。此外,本發明將二氧化矽原料及鋁渣粉末透過微波輔助水熱合成方法製得一沸石,之後再將沸石與異丙醇鈦透過溶膠凝膠法及微波輔助水熱合成方法以製得一複合材料吸附劑,據此,本發明利用微波輔助水熱合成方法可有效地縮短複合材料吸附劑之製程,並使二氧化鈦光觸媒均勻覆蓋於沸石之表面,複合材料吸附劑可透過光照而使二氧化鈦光觸媒進行光催化反應,進而使複合材料吸附劑能有效地且持續地吸附空氣污染物,而無吸附飽和之問題。再者,本發明之複合材料吸附劑以該複合材料吸附劑之總重量計,沸石及二氧化鈦光觸媒之重量比係介於3:7與7:3之間,且複合材料吸附劑能有效地吸附二氧化碳、一氧化碳、甲醛、乙醛、苯酚或其組合。The preparation method of the composite adsorbent of the present invention uses waste glass and waste aluminum slag to prepare silicon dioxide raw materials and aluminum slag powder, respectively, so that the glass and waste aluminum slag can be recycled and reused, thereby avoiding environmental damage and achieving environmental protection The purpose. In addition, in the present invention, a zeolite is prepared from the silicon dioxide raw material and aluminum slag powder through the microwave-assisted hydrothermal synthesis method, and then the zeolite and titanium isopropoxide are prepared through the sol-gel method and the microwave-assisted hydrothermal synthesis method to obtain a zeolite. Composite material adsorbent. According to this, the microwave-assisted hydrothermal synthesis method of the present invention can effectively shorten the preparation process of composite material adsorbent and make the titanium dioxide photocatalyst evenly cover the surface of zeolite. The composite material adsorbent can make the titanium dioxide photocatalyst through light. The photocatalytic reaction is carried out so that the composite adsorbent can effectively and continuously adsorb air pollutants without the problem of adsorption saturation. Furthermore, the composite material adsorbent of the present invention is based on the total weight of the composite material adsorbent. The weight ratio of zeolite and titanium dioxide photocatalyst is between 3:7 and 7:3, and the composite material adsorbent can effectively adsorb Carbon dioxide, carbon monoxide, formaldehyde, acetaldehyde, phenol, or combinations thereof.

以下係藉由特定之具體實施例說明本發明之實施方式,熟習此技術之人士可藉由本說明書所揭示之內容瞭解本發明之其他優點與功效。然而,本發明中所揭示之例示性實施例僅出於說明之目的,不應被視為限制本發明之範圍。換言之,本發明亦可藉由其他不同的具體實施例加以施行或應用,本說明書中的各項細節亦可基於不同的觀點與應用,在不悖離本發明之精神下進行各種修飾與變更。The following is a specific embodiment to illustrate the implementation of the present invention. Those familiar with this technology can understand other advantages and effects of the present invention from the content disclosed in this specification. However, the exemplary embodiments disclosed in the present invention are for illustrative purposes only and should not be construed as limiting the scope of the present invention. In other words, the present invention can also be implemented or applied by other different specific embodiments, and various details in this specification can also be based on different viewpoints and applications, and various modifications and changes can be made without departing from the spirit of the present invention.

除非本文另有說明,否則說明書及所附申請專利範圍中所使用之單數形式「一」及「該」包括複數個體。除非本文另有說明,否則說明書及所附申請專利範圍中所使用之術語「或」包括「及/或」之含義。Unless otherwise stated herein, the singular forms "a" and "the" used in the specification and the appended patent application include plural entities. Unless otherwise stated herein, the term "or" used in the specification and the appended claims includes the meaning of "and/or".

實施例1 複合材料吸附劑之製備方法Example 1" Preparation method of composite adsorbent

參見第1圖,製備複合材料吸附劑之步驟包括: S1:利用破碎機將已破碎的玻璃器皿及燒杯進行破碎並過篩,以得到一玻璃粉末,將10克玻璃粉末加入30毫升3M HCl溶液中,於60°C下攪拌2小時,並透過真空過濾,以得到一第一固相材料;之後,將該第一固相材料加入30毫升4M H 2SO 4溶液中,在60°C下進行攪拌2小時,經真空過濾後,第一固相材料以去離子水沖洗,置入105°C烘箱內進行乾燥24小時,以得到一白色細粉狀之二氧化矽原料; S2:將10克廢鋁渣加入30毫升0.001M H 2SO 4溶液中,於60°C下攪拌2小時,並透過真空過濾,以得到一第二固相材料;以去離子水沖洗該第二固相材料後,置入105°C烘箱內進行乾燥24小時,以得到一鋁渣粉末; S3:將18克二氧化矽原料與10克鋁渣粉末加入30毫升3 M的氫氧化鈉溶液中,於室溫下攪拌24小時,以得到一混合物;將該混合物置於密閉式微波消化器(型號:CEM MARS 6,CEM公司,美國)內,於150°C下進行微波輔助水熱合成反應15分鐘,並透過真空過濾,以得到一第三固相材料,將該第三固相材料置入105°C烘箱內進行乾燥24小時,以得到一沸石;以及, S4:透過溶膠凝膠法,將0.5克沸石與0.5克異丙醇鈦浸於10毫升乙醇溶液中,並攪拌均勻;之後加入10毫升去離子水,於室溫下攪拌24小時,以得到一白色凝膠狀物質;將該白色凝膠狀物質置入105°C烘箱內進行乾燥24小時,以得到一結晶物;將該結晶物置入密閉式微波消化器內,於100°C下進行微波10分鐘,以得到一具有沸石及二氧化鈦光觸媒之複合材料吸附劑。 Referring to Figure 1, the steps of preparing the composite adsorbent include: S1: Use a crusher to crush and siev the broken glassware and beaker to obtain a glass powder, add 10 grams of glass powder to 30 ml of 3M HCl solution After stirring for 2 hours at 60°C and filtering through vacuum, a first solid phase material was obtained; after that, the first solid phase material was added to 30 ml of 4M H 2 SO 4 solution at 60°C Stir for 2 hours. After vacuum filtration, the first solid phase material is rinsed with deionized water and placed in an oven at 105°C for drying for 24 hours to obtain a white fine powdered silicon dioxide raw material; S2: 10 One gram of waste aluminum slag was added to 30 ml of 0.001MH 2 SO 4 solution, stirred at 60°C for 2 hours, and filtered through vacuum to obtain a second solid phase material; after rinsing the second solid phase material with deionized water , Placed in an oven at 105°C and dried for 24 hours to obtain an aluminum slag powder; S3: Add 18 grams of silicon dioxide raw material and 10 grams of aluminum slag powder to 30 ml of 3 M sodium hydroxide solution, at room temperature Stir for 24 hours to obtain a mixture; place the mixture in a closed microwave digester (model: CEM MARS 6, CEM Company, USA), carry out microwave-assisted hydrothermal synthesis reaction at 150°C for 15 minutes, and Vacuum filtration to obtain a third solid phase material, which is placed in an oven at 105°C for drying for 24 hours to obtain a zeolite; and, S4: through a sol-gel method, 0.5 g The zeolite and 0.5 g of titanium isopropoxide were immersed in 10 ml of ethanol solution and stirred evenly; then 10 ml of deionized water was added, and the mixture was stirred at room temperature for 24 hours to obtain a white gel-like substance; The crystalline substance was placed in an oven at 105°C for drying for 24 hours to obtain a crystal; the crystal was placed in a closed microwave digester and microwaved at 100°C for 10 minutes to obtain a photocatalyst with zeolite and titanium dioxide The composite adsorbent.

實施例2 分析沸石之晶相及結構Example 2 Analyze the crystal phase and structure of zeolite

利用X光繞射分析儀(X-ray diffraction, XRD, 型號:Bruker D8)進行步驟S3所得到之沸石之晶相的定性分析,結果如第2圖所示,沸石在繞射角2θ = 6°、10°、12°、15.5°、18.5°、20°、23.5°、26.5°、30°、30.5°、31°、32°、33.5°處出現峰值,顯示沸石係屬於X型沸石。Use X-ray diffraction analyzer (XRD, model: Bruker D8) to perform qualitative analysis of the crystal phase of zeolite obtained in step S3. The result is shown in Figure 2. The zeolite has a diffraction angle of 2θ = 6 There are peaks at °, 10°, 12°, 15.5°, 18.5°, 20°, 23.5°, 26.5°, 30°, 30.5°, 31°, 32°, 33.5°, indicating that the zeolite system belongs to type X zeolite.

利用掃描式顯微鏡(scanning electron microscope, SEM, 型號:FEI Quanta 200)在4000倍之放大倍率下觀察步驟S3所得到之沸石的表面結構,如第3圖所示,結果顯示沸石之表面具有許多粒徑尺寸相近之顆粒,且各顆粒之間存在許多孔隙,使得沸石之比表面積得以被提升。Use a scanning electron microscope (SEM, model: FEI Quanta 200) to observe the surface structure of the zeolite obtained in step S3 at a magnification of 4000 times. As shown in Figure 3, the result shows that the surface of the zeolite has many particles. Particles with similar diameters, and there are many pores between the particles, so that the specific surface area of the zeolite can be increased.

實施例3 分析複合材料吸附劑之元素組成Example 3 Analyze the elemental composition of the composite adsorbent

利用能量分散式光譜儀(energy dispersive spectrometer, EDS, 型號:FEI Quanta 200)分析步驟S4所得到之複合材料吸附劑之元素(Si)、鋁(Al)及鈦(Ti)的組成,如第4圖所示,結果顯示複合材料吸附劑中所含之元素矽(Si)及鋁(Al)的原子量比值約為1:1,因此,複合材料吸附劑係屬於低矽量之沸石配比。低矽量之沸石有相當良好的陽離子交換能力,且對於極性分子具有較佳的電子親和力。Use energy dispersive spectrometer (EDS, model: FEI Quanta 200) to analyze the composition of the elements (Si), aluminum (Al) and titanium (Ti) of the composite adsorbent obtained in step S4, as shown in Figure 4 As shown, the results show that the atomic weight ratio of the elements silicon (Si) and aluminum (Al) contained in the composite adsorbent is about 1:1. Therefore, the composite adsorbent is a zeolite with a low silicon content. Zeolite with low silicon content has quite good cation exchange capacity, and has better electron affinity for polar molecules.

實施例4 檢測複合材料吸附劑吸附空氣污染物之能力Example 4 Detecting the ability of composite adsorbents to adsorb air pollutants

本實施例所檢測之空氣污染物係以甲醛作為示例,檢測沸石、光觸媒以及複合材料吸附劑吸附甲醛之能力。分別將0.5克沸石、光觸媒以及複合材料吸附劑(照射光或未照射光)置於含有1.0 ppm起始濃度之甲醛且相對濕度為45%之抽風櫃內2小時,並於不同的時間點檢測抽風櫃內之甲醛濃度。如第5圖所示,結果顯示於第20分鐘時,相較於沸石、光觸媒及未經光照射之複合材料吸附劑,經光照射之複合材料吸附劑具有更佳地吸附甲醛之能力,且於吸附第2小時後,沸石、光觸媒以及複合材料吸附劑(照射光)之甲醛去除率分別為0%、92.4%及94.9%。顯見,於吸附第2小時後,沸石之吸附能力已達飽而無法繼續吸附甲醛,經光照射之複合材料吸附劑則仍具有良好的吸附甲醛之能力。The air pollutant detected in this embodiment uses formaldehyde as an example to detect the ability of zeolite, photocatalyst, and composite material adsorbent to adsorb formaldehyde. Put 0.5 g of zeolite, photocatalyst and composite material adsorbent (irradiated or unirradiated) in a fume cupboard containing 1.0 ppm initial concentration of formaldehyde and a relative humidity of 45% for 2 hours, and tested at different time points The concentration of formaldehyde in the fume cupboard. As shown in Figure 5, the results show that at the 20th minute, compared with zeolite, photocatalyst, and composite adsorbent without light irradiation, the composite adsorbent irradiated with light has a better ability to adsorb formaldehyde, and After the second hour of adsorption, the formaldehyde removal rates of zeolite, photocatalyst and composite adsorbent (irradiated with light) were 0%, 92.4% and 94.9%, respectively. Obviously, after the second hour of adsorption, the adsorption capacity of zeolite has reached its full capacity and cannot continue to adsorb formaldehyde. The composite adsorbent irradiated by light still has a good formaldehyde adsorption capacity.

實施例5 檢測具有不同比例之沸石及光觸媒之複合材料吸附劑吸附空氣污染物之能力Example 5 Detecting the ability of composite adsorbents with different ratios of zeolite and photocatalyst to adsorb air pollutants

本實施例所檢測之空氣污染物係以甲醛作為示例,檢測具有不同比例之沸石及二氧化鈦光觸媒之複合材料吸附劑吸附甲醛之能力,以複合材料吸附劑之總重量計,所檢測之複合材料吸附劑中的沸石及二氧化鈦光觸媒之重量比分別為3:7、4:6、5:5、6:4及7:3。分別將0.5克之各複合材料吸附劑置於含有1.0 ppm起始濃度之甲醛且相對濕度為45%之抽風櫃內2小時,並照射光後於不同的時間點檢測抽風櫃內之甲醛濃度。如第6圖所示,結果顯示於吸附第2小時後,比例分別為3:7、4:6、5:5、6:4及7:3之複合材料吸附劑之甲醛去除率分別為94.9%、90.5%、86.0%、83.1%及78.7%。顯見,於吸附第2小時後,二氧化鈦光觸媒含量越高之複合材料吸附劑具有更佳的吸附甲醛之能力。The air pollutants tested in this embodiment are based on formaldehyde as an example. The ability of composite adsorbents with different ratios of zeolite and titanium dioxide photocatalyst to adsorb formaldehyde is tested. The total weight of the composite adsorbent is calculated based on the total weight of the composite adsorbent. The weight ratios of zeolite and titanium dioxide photocatalyst in the agent are 3:7, 4:6, 5:5, 6:4 and 7:3, respectively. Put 0.5 g of each composite adsorbent in a fume cabinet containing 1.0 ppm initial concentration of formaldehyde and a relative humidity of 45% for 2 hours, and irradiate light to detect the concentration of formaldehyde in the fume cabinet at different time points. As shown in Figure 6, the results show that after the second hour of adsorption, the formaldehyde removal rates of composite adsorbents with ratios of 3:7, 4:6, 5:5, 6:4 and 7:3 were 94.9. %, 90.5%, 86.0%, 83.1% and 78.7%. Obviously, after the second hour of adsorption, the composite adsorbent with a higher content of titanium dioxide photocatalyst has a better ability to adsorb formaldehyde.

實施例6 檢測不同劑量之複合材料吸附劑吸附空氣污染物之能力Example 6 "Detecting the ability of different doses of composite adsorbents to adsorb air pollutants

本實施例所檢測之空氣污染物係以甲醛作為示例,檢測不同劑量之複合材料吸附劑吸附甲醛之能力,所檢測之複合材料吸附劑中的沸石及二氧化鈦光觸媒之比例為3:7。分別將0.1克、0.2克、0.3克、0.4克及0.5克之各複合材料吸附劑置於含有1.0 ppm起始濃度之甲醛且相對濕度為45%之抽風櫃內2小時,並照射光後於不同的時間點檢測抽風櫃內之甲醛濃度。如第7圖所示,結果顯示於吸附第2小時後,0.1克至0.5克之各複合材料吸附劑之甲醛去除率分別為79.5%、85.9%、88.7%、92.2%及94.9%。顯見,於吸附第2小時後,劑量越高之複合材料吸附劑具有更佳的吸附甲醛之能力。The air pollutants detected in this embodiment are based on formaldehyde, and the ability of different doses of composite material adsorbents to adsorb formaldehyde is tested. The ratio of zeolite and titanium dioxide photocatalyst in the tested composite material adsorbent is 3:7. Put 0.1g, 0.2g, 0.3g, 0.4g and 0.5g of each composite adsorbent in a fume cupboard containing 1.0 ppm initial concentration of formaldehyde and a relative humidity of 45% for 2 hours, and irradiate them with light. Detect the formaldehyde concentration in the ventilation cabinet at the time point. As shown in Figure 7, the results show that after the second hour of adsorption, the formaldehyde removal rate of each composite adsorbent of 0.1 g to 0.5 g was 79.5%, 85.9%, 88.7%, 92.2% and 94.9%, respectively. Obviously, after the second hour of adsorption, the composite adsorbent with higher dosage has better capacity to adsorb formaldehyde.

實施例7 檢測室內不同之相對溫度對於複合材料吸附劑吸附空氣污染物之能力的影響Example 7 Detecting the influence of different relative temperatures in the chamber on the ability of composite adsorbents to adsorb air pollutants

本實施例所檢測之空氣污染物係以甲醛作為示例,檢測室內不同之相對溫度對於複合材料吸附劑吸附空氣污染物之能力的影響,所檢測之複合材料吸附劑中的沸石及二氧化鈦光觸媒之比例為3:7。將0.5克之複合材料吸附劑置於含有1.0 ppm起始濃度之甲醛且相對濕度分別為45%、55%、65%、75%及85%之抽風櫃內2小時,並照射光後於不同的時間點檢測抽風櫃內之甲醛濃度。如第8圖所示,結果顯示於吸附第2小時後,複合材料吸附劑對於相對濕度分別為45%、55%、65%、75%及85%之抽風櫃的甲醛去除率分別為94.9%、95.2%、95.5%、95.8%及96.2%。顯見,於吸附第2小時後,室內不同之相對溫度並不會影響複合材料吸附劑吸附甲醛之能力。The air pollutants detected in this embodiment are based on formaldehyde. The effect of different relative temperatures in the room on the ability of the composite adsorbent to adsorb air pollutants is tested, and the ratio of zeolite and titanium dioxide photocatalyst in the detected composite adsorbent It is 3:7. Put 0.5g of composite material adsorbent in a fume cupboard containing 1.0 ppm initial concentration of formaldehyde and relative humidity of 45%, 55%, 65%, 75% and 85% respectively for 2 hours. Detect the formaldehyde concentration in the ventilation cabinet at the time point. As shown in Figure 8, the results show that after the second hour of adsorption, the composite adsorbent has a formaldehyde removal rate of 94.9% for the exhaust cabinets with relative humidity of 45%, 55%, 65%, 75%, and 85%. , 95.2%, 95.5%, 95.8% and 96.2%. Obviously, after the second hour of adsorption, different relative temperatures in the room did not affect the ability of the composite adsorbent to adsorb formaldehyde.

實施例8 檢測室內不同之空氣污染物之起始濃度對於複合材料吸附劑吸附空氣污染物之能力的影響Example 8 Detecting the influence of the initial concentration of different air pollutants in the room on the ability of the composite adsorbent to adsorb air pollutants

本實施例所檢測之空氣污染物係以甲醛作為示例,檢測室內不同之空氣污染物之起始濃度對於複合材料吸附劑吸附空氣污染物之能力的影響,所檢測之複合材料吸附劑中的沸石及二氧化鈦光觸媒之比例為3:7。將0.5克之複合材料吸附劑置於含有1.0 ppm、0.9 ppm、0.8 ppm、0.7 ppm及0.6 ppm起始濃度之甲醛且相對濕度為45%之抽風櫃內2小時,並照射光後於不同的時間點檢測抽風櫃內之甲醛濃度。如第9圖所示,結果顯示於吸附第2小時後,複合材料吸附劑對於起始濃度分別為1.0 ppm及0.6 ppm之甲醛的甲醛去除率分別為94.9%及89.8%。顯見,於吸附第2小時後,複合材料吸附劑在含有較高之甲醛起始濃度之室內具有更佳的吸附甲醛之能力。The air pollutants tested in this embodiment are based on formaldehyde. The initial concentration of different air pollutants in the room is tested for the effect of the composite adsorbent's ability to adsorb air pollutants. Zeolite in the tested composite adsorbent And the ratio of titanium dioxide photocatalyst is 3:7. Place 0.5 g of composite material adsorbent in a fume cupboard containing 1.0 ppm, 0.9 ppm, 0.8 ppm, 0.7 ppm and 0.6 ppm initial concentrations of formaldehyde and a relative humidity of 45% for 2 hours, and irradiate them at different times Point to detect the concentration of formaldehyde in the ventilation cabinet. As shown in Figure 9, the results show that after the second hour of adsorption, the formaldehyde removal rate of the composite adsorbent for the initial concentrations of 1.0 ppm and 0.6 ppm of formaldehyde were 94.9% and 89.8%, respectively. Obviously, after the second hour of adsorption, the composite adsorbent has a better ability to adsorb formaldehyde in a room containing a higher initial concentration of formaldehyde.

S1:步驟1 S2:步驟2 S3:步驟3 S4:步驟4S1: Step 1 S2: Step 2 S3: Step 3 S4: Step 4

第1圖係本發明之複合材料吸附劑之製備方法的流程圖。 第2圖係本發明之複合材料吸附劑之製備方法中所製得之沸石之晶相的繞射角2θ峰值。 第3圖係本發明之複合材料吸附劑之製備方法中所製得之沸石的表面結構照片。 第4圖係本發明之複合材料吸附劑之元素組成結果圖。 第5圖係本發明之複合材料吸附劑、沸石及光觸媒吸附甲醛之結果圖。 第6圖係本發明之複合材料吸附劑在含有不同重量比之沸石及二氧化鈦光觸媒下吸附甲醛之結果圖。 第7圖係本發明之複合材料吸附劑在不同劑量下吸附甲醛之結果圖。 第8圖係本發明之複合材料吸附劑在不同濕度下吸附甲醛之結果圖。 第9圖係本發明之複合材料吸附劑在不同甲醛之起始濃度下吸附甲醛之結果圖。 Figure 1 is a flow chart of the preparation method of the composite adsorbent of the present invention. Figure 2 is the 2θ peak of the diffraction angle of the crystal phase of the zeolite prepared in the method for preparing the composite adsorbent of the present invention. Figure 3 is a photograph of the surface structure of the zeolite prepared in the method for preparing the composite adsorbent of the present invention. Figure 4 is a diagram showing the elemental composition results of the composite adsorbent of the present invention. Figure 5 is a graph showing the result of adsorption of formaldehyde by the composite adsorbent, zeolite and photocatalyst of the present invention. Figure 6 is a graph showing the results of adsorption of formaldehyde by the composite material adsorbent of the present invention containing different weight ratios of zeolite and titanium dioxide photocatalyst. Figure 7 is a graph showing the results of adsorption of formaldehyde by the composite adsorbent of the present invention under different dosages. Figure 8 is a graph showing the results of adsorption of formaldehyde by the composite adsorbent of the present invention under different humidity. Figure 9 is a graph showing the results of adsorption of formaldehyde by the composite material adsorbent of the present invention under different initial concentrations of formaldehyde.

S1:步驟1 S1: Step 1

S2:步驟2 S2: Step 2

S3:步驟3 S3: Step 3

S4:步驟4 S4: Step 4

Claims (10)

一種複合材料吸附劑之製備方法,包括步驟: 提供二氧化矽原料及鋁渣粉末; 將莫耳比範圍為1:1至5:1之該二氧化矽原料與該鋁渣粉末加入1 M至5 M氫氧化鈉溶液中,混合均勻,以得到一混合物;將該混合物置於一密閉式微波消化器內,於90°C至250°C下進行微波輔助水熱合成反應3分鐘至60分鐘後進行真空過濾,以得到一第三固相材料;將該第三固相材料進行乾燥,以得到一沸石;以及 將重量比範圍為1:5至1:10之該沸石與異丙醇鈦浸於乙醇溶液中,並攪拌均勻;之後加入去離子水並攪拌,以得到一白色凝膠狀物質;將該白色凝膠狀物質進行乾燥,以得到一結晶物;將該結晶物置入該密閉式微波消化器內,於90°C至250°C下進行微波輔助水熱合成反應3分鐘至60分鐘,以得到一複合材料吸附劑。 A preparation method of composite material adsorbent, including the steps: Provide silicon dioxide raw materials and aluminum slag powder; Add the silicon dioxide raw material and the aluminum slag powder with a molar ratio ranging from 1:1 to 5:1 into a 1 M to 5 M sodium hydroxide solution, and mix them uniformly to obtain a mixture; In a closed microwave digester, microwave-assisted hydrothermal synthesis reaction is performed at 90°C to 250°C for 3 minutes to 60 minutes, and then vacuum filtration is performed to obtain a third solid phase material; Drying to obtain a zeolite; and Dip the zeolite and titanium isopropoxide with a weight ratio ranging from 1:5 to 1:10 in an ethanol solution and stir evenly; then add deionized water and stir to obtain a white gelatinous substance; The gelatinous substance is dried to obtain a crystal; the crystal is placed in the closed microwave digester, and the microwave-assisted hydrothermal synthesis reaction is performed at 90°C to 250°C for 3 minutes to 60 minutes to obtain A composite adsorbent. 如請求項1所述之製備方法,其中在提供該二氧化矽原料之步驟中,包括步驟: 將一玻璃粉末加入2M至4M HCl溶液中,於50°C至70°C下攪拌後進行真空過濾,以得到一第一固相材料; 以及將該第一固相材料加入3M至5M H 2SO 4溶液中,於50°C至70°C下攪拌後進行真空過濾,再以去離子水沖洗後進行乾燥,以得到該二氧化矽原料。 The preparation method according to claim 1, wherein the step of providing the silicon dioxide raw material includes the steps of: adding a glass powder to a 2M to 4M HCl solution, stirring at 50°C to 70°C, and vacuuming Filtering to obtain a first solid phase material; and adding the first solid phase material to a 3M to 5M H 2 SO 4 solution, stirring at 50°C to 70°C, vacuum filtration, and then deionized water After rinsing, drying is performed to obtain the silicon dioxide raw material. 如請求項1所述之製備方法,其中在提供該鋁渣粉末之步驟中,包括步驟: 將一廢鋁渣加入0.0001M至0.01M H 2SO 4溶液中,於50°C至70°C下攪拌後進行真空過濾,以得到一第二固相材料;以及 以去離子水沖洗該第二固相材料後進行乾燥,以得到該鋁渣粉末。 The preparation method according to claim 1, wherein the step of providing the aluminum slag powder includes the steps of: adding a waste aluminum slag to a 0.0001M to 0.01MH 2 SO 4 solution at 50°C to 70°C After stirring, vacuum filtration is performed to obtain a second solid phase material; and the second solid phase material is rinsed with deionized water and then dried to obtain the aluminum slag powder. 如請求項1所述之製備方法,其中該微波輔助水熱合成反應係在100°C至220°C下進行10分鐘至50分鐘。The preparation method according to claim 1, wherein the microwave-assisted hydrothermal synthesis reaction is carried out at 100°C to 220°C for 10 minutes to 50 minutes. 如請求項1所述之製備方法,其中該微波輔助水熱合成反應係在100°C至180°C下進行10分鐘至30分鐘。The preparation method according to claim 1, wherein the microwave-assisted hydrothermal synthesis reaction is carried out at 100°C to 180°C for 10 minutes to 30 minutes. 如請求項1所述之製備方法,其中該微波輔助水熱合成反應係在100°C至140°C下進行10分鐘至20分鐘。The preparation method according to claim 1, wherein the microwave-assisted hydrothermal synthesis reaction is carried out at 100°C to 140°C for 10 minutes to 20 minutes. 如請求項1所述之製備方法,其中該微波輔助水熱合成反應係在100°C下進行10分鐘。The preparation method according to claim 1, wherein the microwave-assisted hydrothermal synthesis reaction is carried out at 100°C for 10 minutes. 一種如請求項1至7項中任一項所述之複合材料吸附劑之製備方法所製得之複合材料吸附劑,包括沸石及二氧化鈦光觸媒,其中以該複合材料吸附劑之總重量計,該沸石及該二氧化鈦光觸媒之重量比係介於3:7與7:3之間。A composite adsorbent prepared by the method for preparing a composite adsorbent according to any one of claims 1 to 7, comprising a zeolite and a titanium dioxide photocatalyst, wherein based on the total weight of the composite adsorbent, the The weight ratio of the zeolite and the titanium dioxide photocatalyst is between 3:7 and 7:3. 如請求項8所述之複合材料吸附劑,其中以該複合材料吸附劑之總重量計,該沸石及該二氧化鈦光觸媒之重量比係4:6、5:5或6:4。The composite adsorbent according to claim 8, wherein based on the total weight of the composite adsorbent, the weight ratio of the zeolite and the titanium dioxide photocatalyst is 4:6, 5:5 or 6:4. 一種如請求項8所述之複合材料吸附劑用於吸附空氣污染物之用途,其中該吸附空氣污染物包括二氧化碳、一氧化碳、甲醛、乙醛、苯酚或其組合。A composite material adsorbent according to claim 8 for adsorbing air pollutants, wherein the adsorbed air pollutants include carbon dioxide, carbon monoxide, formaldehyde, acetaldehyde, phenol or a combination thereof.
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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3178550A1 (en) * 2015-09-03 2017-06-14 Panasonic Intellectual Property Management Co., Ltd. Gas adsorbent and vacuum heat insulation member provided with the same
CN111408342A (en) * 2020-04-27 2020-07-14 北京泷涛环境科技有限公司 High-silicon composite molecular sieve adsorbent for removing VOCs (volatile organic compounds) and preparation method thereof

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3178550A1 (en) * 2015-09-03 2017-06-14 Panasonic Intellectual Property Management Co., Ltd. Gas adsorbent and vacuum heat insulation member provided with the same
CN111408342A (en) * 2020-04-27 2020-07-14 北京泷涛环境科技有限公司 High-silicon composite molecular sieve adsorbent for removing VOCs (volatile organic compounds) and preparation method thereof

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