TWI262896B - Process for preparing porous silica xerogel - Google Patents

Process for preparing porous silica xerogel Download PDF

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TWI262896B
TWI262896B TW93138123A TW93138123A TWI262896B TW I262896 B TWI262896 B TW I262896B TW 93138123 A TW93138123 A TW 93138123A TW 93138123 A TW93138123 A TW 93138123A TW I262896 B TWI262896 B TW I262896B
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gel
hours
modified
wet gel
porous
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TW93138123A
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TW200619142A (en
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Yu-Cheng Chang
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Ind Tech Res Inst
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Abstract

The present invention discloses a process for preparing silica xerogel including 2-step acid-base catalyst procedures, a surface modification with trimethylchlorosilane, and a heat treatment at a high temperature. The 2-step acid-base catalyst procedures includes mixing tetraethoxysilane, isopropanol, water and acid to form a sol solution, and adding an aqueous solution of ammonium hydroxide to start gelation.

Description

1262896 九、發明說明: 發明所屬之技術領域 、本發明係關於一種多孔性二氣化石夕乾凝膠的製備方 法,尤其有關—種利用溶膠-凝膠法及表面改質的多孔性二 氧化矽乾凝膠的萝偌古土 lL . p &備方法。此多孔性二氧化矽乾凝膠可用 作為熱絕緣材料。 先前技術 習知二氧化石夕凝膠主要製程方式,是以溶膠凝膠法製 備而成,基本上溶膠凝膠法是一種液相的化學反應機制,、 猎由無機鹽類(inorganie saIts)、有機鹽類(。啊k 、 烧氧化物⑽〇xide)'金屬氧化物(metal〇xides)之前躺物 與各種不同溶劑,將各種藥品根據不同比例(濃 度、純度),進行混合攪拌一定時間後,得到我們所 化石夕溶膠溶液。但是,溶膠凝膠塊材體容易因為製程方式 ,不同,而導致塊材體破裂且製程參數控制不易,因此^ 製備二氧化矽凝膠將需考量於不同狀態下,決定適合 膠綾膠製程方式,以利得到高性能之凝膠隔熱材。1262896 IX. Description of the invention: The technical field to which the invention belongs, and the present invention relates to a method for preparing a porous two-gas fossil shower gel, in particular to a porous cerium oxide using a sol-gel method and surface modification. Dry gel of the radix lozenge lL. p & preparation method. This porous ceria xerogel can be used as a thermal insulating material. The main process of the prior art is that the sol-gel method is prepared by a sol-gel method. Basically, the sol-gel method is a chemical reaction mechanism of a liquid phase, and the inorganic salt (inorganie saIts) is used for hunting. Organic salt (. ah k, burnt oxide (10) 〇xide) 'metal oxide (metal 〇xides) before lying with a variety of different solvents, various drugs according to different ratios (concentration, purity), mixing and stirring for a certain period of time , get our fossil sol solution. However, the sol-gel block body is easy to be broken due to the different process methods, and the block material is broken and the process parameters are not easy to control. Therefore, the preparation of the cerium oxide gel will need to be considered in different states, and it is determined that it is suitable for the rubber glue process. In order to obtain high performance gel insulation.

一般利用溶凝膠法製作玻璃或陶瓷時,多以矽烷氧化 物(siloxane)為最常使用的前驅物,矽烷氧化物之化學H 表示為Si(〇R)4,其中以代表烷基。其溶凝膠製程主要分為1 水解、縮聚合三個步驟: '' I 水解反應(Hydrolysis Reaction) 矽烷氧化物中之一 〇R基與水反應,此類物質大八〜 刀容 1262896 易水解成氫氧化物,水分子中之一 OH基取代一 OR基而形 成含有一 0H基之矽烷氧化物,並釋出醇類,前驅物以(〇11)4 與水攪拌後,以酸或鹼催化下進行水解,其化學反應機制 如下所示:When glass or ceramics are generally produced by a lyotropic method, siloxane is most commonly used as a precursor, and the chemical H of the decane oxide is represented by Si(〇R)4, which represents an alkyl group. The lyophilization process is mainly divided into three steps of hydrolysis and condensation polymerization: '' I Hydrolysis Reaction One of the decane oxides reacts with hydrazine and reacts with water. These substances are large VIII ~ 刀容1262896 a hydroxide, one of the water molecules OH group is substituted with an OR group to form a decyl oxide containing a 0H group, and the alcohol is released, and the precursor is stirred with water ((11)4) with acid or alkali. Hydrolysis is carried out under catalysis, and the chemical reaction mechanism is as follows:

(R0)3SiOR + 4//20 <=> HOSi(OR)3^R〇H ^>Si(OH)A +4R0H (1) 鈾驅物以四乙氧基石夕燒$ζ·… (tetraethylorthosilicate,or tetraethoxysilane,簡稱 TEOS)而(R0)3SiOR + 4//20 <=> HOSi(OR)3^R〇H ^>Si(OH)A +4R0H (1) Uranium flooding with tetraethoxy zebra burning $ζ·... (tetraethylorthosilicate, or tetraethoxysilane, referred to as TEOS)

Si(OC2H5)4 +4H20 Si(OH)4 +4C2H5OH (2) 2·给百 (Condensation Reaction) 經過水解的Si(OR)4會與另一 si(〇R)4進行縮合以形成 (OH)3Si-0-Si(OH)3並脫出一水分子,其中,由上式(2)中, 石夕酸(monosilicic acid)經由縮合反應,可形成二氧化矽濕凝 膠·· nSi{OH、* —> viSiO0 + ILyiH^O (3 ) 3.聚合反應 I合反應在親核性取代機構(nucleophilic substitution) 中,由於氫氧基或烷氧基攻擊所造成之親性加成 (nucleophilic addition)作用,其中含有氫氧基的矽烷氧化 物,容易與其他烷氧物中之烷氧基或氫氧基繼續反應形成 架鍵橋(bridging oxygen)而釋放出醇或水份,如以下反應式 所示,(0H)3Si-0-Si(0H)3將會與其他的si(〇H)4進行聚合形 成二氧化矽網狀結構之聚合物所有的反應可以利用酸或鹼 1262896 來催化 有所不 ,在不同催化條件 同。 下所產生的溶凝膠在結構上也會 H〇-—·Si^一q—Si— Oil I I ^ 〇 OH 1,0—ψ一O—si—0—Si— OH i L I HO—〇H H〇一sj_ 0II — 加 ου 、”有:而。.體粒子的大小、結構、交聯度與溶膠的 «度有極深的關係,因 凝膠 Μ切和^合的反應速率控制著溶 脾佔月間,上述任何一項若發生改變, 將使付起始溶液的組成 ^ 變成相八& 成么生艾化。讓原本的均勻溶液因此 劑置的多窠,合嬗、、六、、六I m ^ 影塑凝豚士 B 之反應物的濃度產生變化,明顯地 曰:一間的長短和凝膠的顯微結構。 广I化矽/旋膠製程參數主要以前驅物、溶劑、水、 及不同改質劑之相對莫耳比例,亦為凝膠熱性質影 曰口之―,惟在製備過程中常發現下列問題: :使用不同的溶劑’溶液的表面屋力及點度將受到不 、衫響,因而造成凝膠製備程序中凝膠化之重要参數。 _ 2· S〗(0R)4具有不同烷基(R)的凝膠化時間,當選擇不 ^的燒基時,對於鏈變長或形狀複雜會降低縮合:應的機 ^ 卩♦低形成網狀結構聚合物之比例。 3.早期Kistler等人’發現先利用水將凝膠中的鹽分洗Si(OC2H5)4 +4H20 Si(OH)4 +4C2H5OH (2) 2·Condensation Reaction The hydrolyzed Si(OR)4 will condense with another si(〇R)4 to form (OH) 3Si-0-Si(OH)3 and one molecule of water is removed, wherein, by the condensation reaction of monosilicic acid in the above formula (2), a cerium oxide wet gel··nSi{OH can be formed. , * —> viSiO0 + ILyiH^O (3) 3. Polymerization I-reaction in nucleophilic substitution, nucleophilic due to hydroxyl or alkoxy attack Addition), wherein the oxane oxide containing a hydroxyl group is easily reacted with an alkoxy group or a hydroxyl group in another alkoxide to form a bridging oxygen to release an alcohol or a water, such as the following reaction As shown in the formula, (0H)3Si-0-Si(0H)3 will be polymerized with other si(〇H)4 to form a polymer of ceria network. All reactions can be catalyzed by acid or base 1262896. Something is different in different catalytic conditions. The lyogel produced under the structure will also be H〇--·Si^-q-Si- Oil II ^ 〇OH 1,0—ψ一O—si—0—Si— OH i LI HO—〇HH 〇一sj_ 0II — plus ου , "有:和.. The size, structure, and degree of cross-linking of the bulk particles have a very deep relationship with the degree of the sol. The reaction rate of the gel is cut and the spleen is controlled. In the meantime, if any of the above changes, the composition of the starting solution will be changed to phase VIII and become a smear. Let the original homogeneous solution be sputum, 嬗, 、, The concentration of the reactants of the six I m ^ phantom B is a change, apparently: the length of a room and the microstructure of the gel. The process parameters of the I/旋胶 are mainly precursors, solvents, The relative molar ratio of water and different modifiers is also the result of the thermal properties of the gel. However, the following problems are often found during the preparation process: The surface potential and the degree of the solution using different solvents will be affected. No, the shirt is ringing, thus causing an important parameter for gelation in the gel preparation process. _ 2· S (0R) 4 has a different alkyl (R) Gelation time, when the choice of non-burning base, the chain lengthening or complex shape will reduce the condensation: the machine should be 卩 ♦ low to form the proportion of the network structure polymer. 3. Early Kistler et al. Water washes the salt in the gel

0H0H

0H H0 —Si一 〇一si〜〇H0H H0 —Si—〇一si~〇H

0H0H

0H 'η H20 1262896 去除卩以醇將水父換出來,最後將醇蒸發掉,如此六尤 可產生凝勝。但因為濕態氧化石夕凝膠内溶劑若以簡單的: 熱乾燥方式去除,凝朦骨架會產生收縮,使得凝膠碎裂。口 此種現象是凝膠多孔狀固體在溶劑蒸發時無法承受來 礼界面強大表面張力,以致孔洞崩塌所致。 ‘ 劑!的多寡’會使得溶液中反應物濃度產生變 ”嚴重影響凝膠時間與顯微結構。 好英國㈣682574 (西元1952年)揭示一種疏水性的二 产改所” I括將具有一個或兩個d-C4烧基的氣化石夕 -貝^於一惰性溶劑中與二氧化石夕粒子反應。 發明内容 本發明針對㈣凝膠製程參數例如前驅物、溶劑 ==改!劑的種類及它們之相對莫耳比例進行調 "氧化矽/旋膠化與時效(aging)處理的效率, =孔隙内表面張力所產生之破裂現象的發生與降低孔 本發明接+ ϋ 種網狀結構二氧化矽乾凝膠的製備 / 包含·利用碎掠惫仏rb 槪屯知 7氚虱化物中之一 〇R基與水反應,以趟酸 做為酸催化劑, 、疋水解成矽氫氧化物(矽溶膠),再以氨 水做為鹼催化劑, 八2 進仃縮合反應以形成-Si-O-Si-並放出水 刀子,於是得到-& 劑(溶於正己貌中^化石夕濕凝膠,再以三甲基氯石夕院改質 二童A h *兀,進行表面改質,引入所需之官能基於 羊匕化取表面,卩左 思之利用高溫煅燒,形成隔熱性網狀結構 1262896 一氧化碎乾凝膠。 本發明的矽溶膠的製備係使用莫耳比例為丨:X: 2: 1.8X10-3之四乙氧基矽烷(以⑴匕仏)4)、異丙醇 (ch3ch(qh)3oh)、去離子水及鹽酸的混合物,其中χ介於 2到12。氨水的用量(莫耳數)約等於鹽酸的用量。由於本 發明使用四乙氧基錢,相較於其它長鏈的耗氧化物, 本發明方法的凝膠時間可大幅縮短。本發明使用異丙醇作 為溶劑,由於其具有一適當的蒸氣壓(25(5C時為a」化㈩, 避免因產生表面張力於凝膠體結構上導致的凝膠體收縮現 象此外’ X介於2到12的異丙醇對四乙氧基矽烷的莫耳 匕”有σ適的膝化時間,太多或太少的異丙醇溶劑都會 導致膠化時間太長。 曰 本^月方法使用改質劑(溶於正己烷中)對濕凝膠進行 表面改貝於疋避免二氧化矽濕凝膠在後績的高溫處理時 發生碎裂的現象。 本毛月方法所製得之網狀結構二氧化矽乾凝膠具有 100至600 m2/g之Βετ比表面積。 實施方式 本發明提出_ ^ -7\ VA ^ 種夕孔性一氣化石夕乾凝膠的製備方法 包括下列步驟: 0製備濕凝膠,包含使一含有四乙氧基矽烷、異丙醇、 水及合物進行水解反應,及於-驗催化劑的存在下 進4丁水‘合反應,而形成濕凝膠,其中該四乙氧基石夕燒對 1262896 異丙醇的莫耳比介於1:2至hl2 · 11)將該濕凝膠浸於一包含一 改所、於该Φ、隹一七 改貝劑與一惰性溶劑的 改貝/合液中進仃表面改質,苴 m Cl Γ4 ^ A AA - /、〜文貝劑為具有一個或兩 個C 1-C4 :!:元基的氣化矽烷 反應性; ““生浴劑係對該改質劑不具 叫熱處理該表面改質過的 氧化矽乾凝膠。 以形成夕孔性一 較佳的,步驟Π)的改質劑為三甲基氣石夕烧。 一,的’步驟Π)的惰性溶劑為正己燒,丙嗣,甲苯, 一氯甲烷或氯仿,以正己烷為更佳。 較佳的,步驟ii)的改質溶液呈 〆h w 欣具有1-20體積%的三甲基 虱矽烷,及該濕凝膠浸於該改質溶液12_72小時。 較佳的’步驟出)的熱處理包含於价至麟加孰 24-96小時;及於⑽。Cn〇〇〇c加熱ΐ ι〇小時。 較佳的,步冑出)所製得的多孔性二氧化石夕乾凝膠具有 100至600 m2/g之BET比表面積。 依本發明的一較佳且體音 1 一骽貝轭例所進行的網狀結構二氧 化石夕乾凝膠的製備方法說明如下: ⑷將1莫耳的四乙氧基石夕貌溶於乂莫耳的異丙醇。 將1.8X10·3莫耳的鹽酸與2莫耳的去離子水混 s於反應槽内犯合上述兩種溶液,以3〇〇 rpm 均質攪拌2 0分鐘。 (b)再將以8.12x1 〇·3莫耳的氫氧化銨與2莫耳的去離 子水配製的加入步驟(a)的溶膠,以3〇〇 RpM均質 10 1262896 搜掉1 〇分鐘。 (C)反應槽以不透氣膜隔絕外界空氣,靜置於^⑻ 、至溫 中,進行凝膠化(gel at ion)程序。當莫耳比例X為 3時,凝膠化靜置40小時;當x為6時,凝腰化 靜置1 10小時;當X為9時,凝膠化靜置126】 時。但若X為1.5,則凝膠化靜置時間長達約76〇 J日^。元成4膠化與時效處理直接形成濕凝脉。 (d) 以6%體積比之三甲基氯矽烷的正己烷溶液進行 溶劑交換/表面改質程序,包括將該濕凝膠靜置於 6 %體積比的三甲基氯矽烷的正己烷溶液中36小 時。 (e) 完成改質後,置於室溫下乾燥48小時。 (f) 將改質後的凝膠(modification gel)於4(rc烘箱内 進行除水吸附20分鐘。 (g) 除水後的凝膠於固定溫度6〇〇c下乾燥48小時。 (h) 將乾燥後的矽凝膠置於坩鍋内,再置於高溫爐中 煅燒,通入空氣以每分鐘rc從室溫升溫至2〇〇 C,再以每分鐘3°C由200°C升溫至600°C,持溫 2小時後,即可得到網狀結構二氧化矽乾凝膠。 當X為3-6時,所製得的網狀結構二氧化矽乾凝膠具 有一密度 0·36 g/cm3,一 BET 比表面積 7〇8·2 m2/g,一孔 隙體積1·8 cm /g,一平均孔洞大小1618埃及熱傳導係數 0.089 W/m-k 〇0H 'η H20 1262896 Remove the hydrazine and replace the water father with alcohol, and finally evaporate the alcohol, so that six can produce a condensate. However, because the solvent in the wet oxidized oxide gel is removed by simple: thermal drying, the condensed skeleton will shrink and the gel will be broken. This phenomenon is caused by the collapse of the hole in the gel porous body when the solvent evaporates and cannot withstand the strong surface tension of the interface. ‘ Agent! The amount of 'will cause the concentration of the reactants in the solution to change' severely affects the gel time and microstructure. Good Britain (4) 682574 (AD 1952) reveals a hydrophobic second-generation reform institute. I will have one or two d The -C4 alkyl-based gasification stone is reacted with the cerium oxide particles in an inert solvent. SUMMARY OF THE INVENTION The present invention is directed to (iv) gel process parameters such as precursors, solvents == change! The type of agent and their relative molar ratio are adjusted. The efficiency of yttria/rotation and aging treatment, the occurrence of rupture caused by the surface tension of the pores and the decrease of the pores. Preparation of reticular cerium oxide xerogel/inclusion·Using crushed 惫仏rb 槪屯 knowing that one of the ruthenium compounds is reacted with water, using citric acid as an acid catalyst, and hydrolyzed into ruthenium Hydroxide (ruthenium sol), then ammonia water as a base catalyst, argon condensation reaction to form -Si-O-Si- and release water knife, thus obtaining -& agent (dissolved in the positive appearance ^ fossil) Xixi wet gel, and then modified with a trimethyl chlorite cherished two children A h * 兀, surface modification, the introduction of the required functional based on the aphid surface, the use of high temperature calcination, the formation of heat insulation Sexual network structure 1262896 oxidized pulverized gel. The cerium sol of the present invention is prepared by using a molar ratio of 丨:X: 2: 1.8X10-3 tetraethoxy decane (by (1) 匕仏) 4), A mixture of isopropanol (ch3ch(qh)3oh), deionized water and hydrochloric acid, wherein χ is between 2 and 12. The amount of ammonia (molar) is approximately equal to the amount of hydrochloric acid. Since the present invention uses tetraethoxyl money, the gel time of the process of the present invention can be substantially shortened compared to other long chain oxides. The present invention uses isopropyl alcohol as a solvent, since it has a suitable vapor pressure (25 (a) at 10C (10), avoiding gel shrinkage caused by surface tension on the gel structure. From 2 to 12, the isopropanol to tetraethoxy decane has a sigma-like knee time, and too much or too little isopropanol solvent will cause the gelation time to be too long. The surface of the wet gel is modified by using a modifier (dissolved in n-hexane) to prevent the cracking of the cerium dioxide wet gel during the high-temperature treatment of the subsequent performance. The cerium oxide xerogel has a Βετ specific surface area of 100 to 600 m 2 /g. Embodiments The present invention provides a method for preparing _ ^ -7 VA ^ species of porphyrin gasification dry gel comprising the following steps: Preparing a wet gel comprising: hydrolyzing a tetraethoxy decane, isopropanol, water and a compound, and forming a wet gel in the presence of a catalyst to form a wet gel, wherein The molar ratio of the tetraethoxy zebra to 1262896 isopropanol is between 1:2 and Hl2 · 11) immersing the wet gel in a modified or modified solution containing Φ, 隹7 modified agent and an inert solvent, 苴m Cl Γ4 ^ A AA - /, ~ Wenbei agent is a gasified decane reactivity with one or two C 1-C4 :!: elementary groups; ""The bathing agent is not modified by heat treatment of the surface modification agent.矽 矽 矽 。 。 以 以 以 以 以 一 一 一 一 一 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 较佳 矽 矽 矽 矽Preferably, the modified solution of step ii) has dimethylhethane having 1-20% by volume of trimethyl decane, and the wet gel is immersed in the chloroform or chloroform. The modified solution is 12-72 hours. The preferred 'step-out' heat treatment is carried out at a price of from lining for 24-96 hours; and at (10) Cn〇〇〇c is heated for 〇 〇 hours. Preferably, stepping out) The porous silica dioxide dry gel produced has a BET specific surface area of 100 to 600 m 2 /g. According to a preferred embodiment of the present invention, a network of knots is performed. The preparation method of the composition of the dioxide dioxide dry gel is as follows: (4) Dissolving 1 mole of tetraethoxylate in isopropyl alcohol. 1.8X10·3 molar hydrochloric acid and 2 molar Deionized water mixed with the above two solutions in the reaction tank, homogenized for 20 minutes at 3 rpm. (b) Then take 8.12x1 〇·3 moles of ammonium hydroxide with 2 moles The sol added to the step (a) prepared by ionized water was searched for 3 262 minutes with 3〇〇RpM homogenization 10 1262896. (C) The reaction tank was insulated from the outside air by a gas-tight membrane, and placed in ^(8) to warm. Gel at ion procedure. When the molar ratio X was 3, gelation was allowed to stand for 40 hours; when x was 6, the waist was allowed to stand for 10 hours; when X was 9, gelation was allowed to stand for 126 times. However, if X is 1.5, the gelation standing time is as long as about 76 〇 J. Yuancheng 4 gelation and aging treatment directly form wet coagulation veins. (d) A solvent exchange/surface modification procedure was carried out in a 6% by volume ratio of trimethylchloromethane in n-hexane, including static solution of the wet gel in a 6 % by volume solution of trimethylchloromethane in n-hexane. 36 hours in the middle. (e) After the modification is completed, it is dried at room temperature for 48 hours. (f) The modified gel was subjected to water removal adsorption for 4 minutes in a 4 (rc oven). (g) The gel after water removal was dried at a fixed temperature of 6 ° C for 48 hours. The dried ruthenium gel is placed in a crucible, and then calcined in a high-temperature furnace, and air is introduced to raise the temperature from room temperature to 2 ° C per minute rc, and then to 200 ° C at 3 ° C per minute. After heating to 600 ° C and holding the temperature for 2 hours, a network structure of cerium oxide xerogel can be obtained. When X is 3-6, the obtained network structure cerium oxide xerogel has a density of 0 · 36 g/cm3, a BET specific surface area of 7〇8·2 m2/g, a pore volume of 1·8 cm / g, an average pore size of 1618 Egypt heat transfer coefficient 0.089 W/mk 〇

Claims (1)

1262896 十、申請專利範圍: 包括下列步 1 · 一種多孔性二氧化矽乾凝膠的製備方法 驟: i) 製備濕凝膠,包含使一含有四乙氣基 上7 ’元、異丙醇、 水及酸的混合物進行水解反應,及於一鹼# 1隹化劑的存在下 進行聚縮合反應,而形成濕凝膠,其中該 ^ W乙氧基矽烷對 異丙醇的莫耳比介於1:2至1:1 2 ; ii) 將該濕凝膠浸於一包含一改質劑盥一卜左κ ^ 惰性溶劑的改 質溶液中進行表面改質,其中該改質劑為呈女 y1262896 X. Patent application scope: The following steps are included: 1. Preparation method of a porous cerium oxide xerogel: i) preparing a wet gel comprising a 7' element, isopropanol, containing a tetraethylene group, The water and acid mixture is subjected to a hydrolysis reaction, and a polycondensation reaction is carried out in the presence of a base #1 hydrating agent to form a wet gel, wherein the molar ratio of the ethoxylated decane to the isopropyl alcohol is between 1:2 to 1:1 2; ii) immersing the wet gel in a modified solution containing a modifier 盥 左 κ ^ inert solvent for surface modification, wherein the modifier is a female y ,、有一個或兩個 c 1-C4 :):完基的氯化石夕烧,該惰性溶劑係對兮所 次p又貝劑不具及 應性; 、久 以形成多孔性二氧 iii)熱處理該表面改質過的濕凝膠 化矽乾凝膠。 2·如申請專利範圍第i項的方法,其中步驟Η)的改林 劑為三甲基氯矽烷。 貝 3·如申請專利範圍第丨或2項的方法,其中步 达 1)的 月性溶劑為正己烷,丙酮,甲苯,二氯甲烷或氯仿。 4·如申請專利範圍第3項的方法,其中該惰性溶劑為 如申請專利範圍第4項的方法,其中步驟Η)的改質 12 1262896 溶液具有1 -20體積%的三甲基氯矽烷,及該濕凝膠浸於該 改質溶液12-72小時。 6 .如申請專利範圍第1項的方法,其中步驟i i i)的熱處 理包含於45°C至10(TC加熱24-96小時;及於100°C至 800°C加熱1-10小時。, one or two c 1-C4 :): the complete chlorinated stone smoldering, the inert solvent is not suitable for the p and the shelling agent; for a long time to form a porous dioxygen iii) heat treatment The surface modified wet gelled dry gel. 2. The method of claim i, wherein the step Η) is a trimethylchloromethane. The method of claim 3 or 2, wherein the monthly solvent of step 1) is n-hexane, acetone, toluene, dichloromethane or chloroform. 4. The method of claim 3, wherein the inert solvent is the method of claim 4, wherein the modified 12 1262896 solution of step Η) has 1 to 20% by volume of trimethylchlorodecane, And the wet gel is immersed in the modified solution for 12-72 hours. 6. The method of claim 1, wherein the heat treatment of step i i i) is carried out at 45 ° C to 10 (TC is heated for 24-96 hours; and heated at 100 ° C to 800 ° C for 1-10 hours). 7.如申請專利範圍第1項的方法,其中步驟iii)所製得 的多孔性二氧化矽乾凝膠具有100至600 m2/g之BET比表 面積。7. The method of claim 1, wherein the porous ceria xerogel prepared in step iii) has a BET specific surface area of from 100 to 600 m2/g. 1313
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