TW315375B - - Google Patents

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TW315375B
TW315375B TW83106013A TW83106013A TW315375B TW 315375 B TW315375 B TW 315375B TW 83106013 A TW83106013 A TW 83106013A TW 83106013 A TW83106013 A TW 83106013A TW 315375 B TW315375 B TW 315375B
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Taiwan
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polyisocyanate
item
aerogel
catalyst
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TW83106013A
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Chinese (zh)
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Ici Plc
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Priority claimed from GB939315198A external-priority patent/GB9315198D0/en
Priority claimed from GB939319451A external-priority patent/GB9319451D0/en
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Publication of TW315375B publication Critical patent/TW315375B/zh

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315375 Α7 Β7 經濟部中央標準局員工消費合作杜印製 五、發明説明(1 ) 本發明係關有機氣凝膠,較明確言之係關多異氰酸酯基 的氣凝膠及其製法。 ~ 多異氰酸酯基的硬泡沫%聚尿烷及聚異氟尿酸酯泡沫等 為技術上所週知’用作絕熱介質例如在冷藏設備的结構内 。&等泡沫一般係由適當多異氰酸酯與多元醇於發泡劑存 在中反應製得。硬泡沫的絕熱性質依賴許多因素,包括閉 泡硬泡沫之氣室大小及氣室内容物之熱導率(即泡沫製法 中所用發泡劑者)。 生產®質聚尿烷及聚異氰尿酸酯泡沫中曾廣用作發泡劑 之一類物質為完全鹵化的含氛氟烴,特別為三氛氟甲烷 (CFC-11)。此等發泡劑之非常低熱専率、尤其cpc-u,能 製備具極有效絕熱性的硬泡沫。近來對氯氟烴類引起耗竭 大氣中臭氣潛力之關注導致迫切要求開發糸統更改能為環 «Ν, 境接受的材料替代氯氟烴發泡劑、,亦製造其中用作多種賁 用有必要性質之泡沫。 Μ往技術上主張的此類其他發泡劑包括氫氛氟烴、氬氟 烴及(環)烷烴等類。此等材料雖比氯氟烀類較能為環境 接受(其臭氧消耗潛力(ODP)較小或甚至零)而涵熱性稍 差。 — 鑒於能源消耗及環境立法之強烈需求,於是探索選擇的 多異氰酸酯基礎之絕熱材料。 此等選擇之一為填充敞泡硬聚知烷泡沫的抽空絕熱板。 利用真空可消除試樣中氣體導熱而減少試樣之熱導。但此 項真空絕熱板之熱導率由於氣體如空氣與水汽在板内部逐 -4- 本纸張尺度適用中國國家標準(CNS ) Α4規格(210X 297公釐) (請先闼讀背面之注意事項再填寫本頁) 袈. 、-* A7 B7 經濟部中央標準局員工消費合作社印製 五、發明説明(2) 漸擴散,隨與時俱增的内在壓力而迅速加大。 氣凝膠以其超级絕緣著稱,乃因摒絕來自氣栢之任何 參與。此等物質因充滿空而善處環境。而且不易老化。 氣凝膠為一獨特類的超细氣室大小、低密度的敞泡泡沫 。#凝膠有持鱭孔隙性,其孔徑低於空氣平均自由通道之 微结構(孔徑在公沙範圍)成為其異常熱性質的原因。 傳统的氣凝膠為無機物(例如矽石、礬土或氧化锆氣凝 膠)經金靥酵鹽之水解及縮合作用製得。 矽石氣.凝膠已開發作例如嵌窗玻璃之超絕熱材料。有機 氣凝膠可望有更低熱導率,因而在絕熱用途中提供較少熱 損失。 近來已發展有機氣凝膠。US專利4997804及4873218號 說明間苯二酚-甲醛氣凝膠。US專利5086085及5081163 麯 號敘述蜜胺-甲醛氣凝膠等。-、 在此以前從未有敘述根據多異氰酸酯化學的有機氣凝膠 。因此本發明之目的在提供根據多異氰酸酯化合之有機氣 凝膠及其製法。於是本發明供應一種多異氰酸酯基礎的有 機氣凝膠。 文内所用多異氰酸酯基礎的〃一辭意諝本發明氣凝躍_ 能具Μ下型式:聚尿烷氣凝膠,聚脲氣凝膠*聚異氰尿酸 酯氣凝膠,聚異氟尿酸酯/聚尿烷氣凝膠,聚腺基甲酸酯 氣凝膠,聚二配位基氣凝膠,聚||二腺氣凝膠。 根據本發明的氣凝膠有小於或等於100 nni的孔徑。一般 孔徑在1至100 nm範圍内,較常在5至50 nm範圍内,更 -5- 本紙张尺度適用中國國家橾隼(CNS ) Μ規格(210 X 297公嫠) (請先閱讀背面之注意事項再填寫本頁) 袈· 訂 315375 A7 _ B7五、發明説明(3 ) 常在5至25 nm範圍内。 孔徑能用透射電子顯薇術.(TEM)或Brunauer-Emmet-Teller氮吸附作用(BET)务汞孔率計量術目視決定。引述 的孔徑值係根撺液氮吸附作用的Micromeritics AS#2000型3.0孔率計系統測定之平均孔隙直徑。平均孔 徑係依4 V/A計算,其中V =每公克材料之累積孔隙度及 A =由5 -點BET測定之比表面積。 本發明氣凝膠的密度一般在1至1000 kg/η3範圍内,較 常在10至800 kg/m3範圍内,更常在20至400 kg/n3或甚 至30至300 kg/m3或甚至90至200 kg/m3範圍內。測量密 度能用秤重及測定沉浸排代水容量、或用秤重及测量一有 規則形狀試樣之幾何體積決定。 本發明氣凝膝的表面積一般在10至1500 m2/g範圍内, 較常在50至1200 m2/g範圍内-、更常在200至1000m2/g或 甚至700到1000 m2/g範圍内。表面積能用例如BET決定 0 本發明的有機多異氰酸酯基氣凝膠可由一多異氰酸酯與 一異氰酸酯三聚作用觸媒在一適當溶劑内混合,保持該混 合物於靜態歷充份長時期生成聚合型凝膠製得。如此作敗 —I m In ..... i HI -I- - HI In 一OJ (請先閱讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印製 異 合三乾 多 化加地 據。性添界 根者活中臨 係學根其超 膠化酸,後 凝酯氰内然 氣酸異劑, 的尿度溶態 得氰能當靜 所異%適於 此多高一物 如的更於合 。 良與丨混 燥改酯胺持 乾烷酸元保 界尿氰多。 臨括異及媒 超包多酵觸 經學解元烷 後化溶多尿 然酷地如及 膝酸擇諸應 凝尿選彳反 的氰 物聚 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) A7 B7 經濟部中央標準局員工消費合作杜印製 五、發明説明 〔4 ' 1 1 I 燦 0 如 此 獲 得 的 氣 凝 膠 係 根 據 聚 尿 烷 與 / 或 聚 腺 化 學 0 此 1 1 1 一 替 換 製 法 容 許 待 用 溶 m 之 較 大 選 擇 並 增 加 膠 凝 時 間 與 乾 1 燦 條 件 之 處 理 内 容 〇 >·* 請 先 1 1 本 氣 凝 膠 的 本 製 法 中 所 用 多 異 氰 酸 酯 包 括 文 獻 内 已 知 製 讀 1 I 造 多* 異 氰 尿 酸 酯 材 料 時 通 用 之 脂 族 環 脂 族 芳 基 脂 族 及 背 面 1 I 之 1 芳 族 多 異 氰 酸 酯 〇 特 別 重 要 者 為 芳 族 多 異 氰 酸 酯 如 甲 次 苯 注 意 1 I 基 及 二 苯 基 甲 烷 二 異 氰 酸 酯 之 周 知 的 純 淨 、 改 良 與 粗 製 式 事 項 1 1 再 I 特 別 為 二 苯 基 甲 惊 二 異 氰 酸 酯 (MDI) 或 其 2, 4 * - 導 2, 2 ' 及-4, 4 ’ - 異 構 體 式 ( 鈍 MD I ) 及 技 術 上 所 知 為 粗 寫 本 頁 袈 1 製 或 聚 合 型 MDI ( 多 亞 甲 多 次 苯 多 異 氰 酸 酷) 有 異 酸 1 I 根 官 能 度 大 於 2 之 混 合 物 及 所 謂 MDI 變 體 者 ( MD I 經 引 進 1 1 尿 烷 腺 基 甲 酸 酯 腺 縮 二 脲 N 碳 化 二 亞 胺 m 酮 醸 亞 1 I 胺 或 異 氰 尿 酸 酯 餘 基 等 改 良 者 ) 〇 訂 在 用 氣 態 溶 劑 ( 如 HCFC 22 的 情 況 中 本 法 製 作 氣 凝 膠 1 I 用 之 多 異 氰 酸 酯 較 佳 係 一 由 多 異 氰 酸 醋 與 一 異 氰 酸 酯 反 應 1 性 化 合 物 製 作 之 所 謂 異 氰 酸 根 末 端 的 預 聚 合 物 0 製 備 此 項 1 | 預 聚 合 物 用 的 異 氰 酸 酯 反 懕 性化 合 物 較 佳 為 一 種 氧 化 亞 烷 如 氧 化 乙 烯 及 / 或 氧 化 丙 烯 與 一 種 單 醇 或 二 元 醇 之 反 應 產 1 物 〇 此 項 羥 烷 單 醇 或 二 元 酵 内 氧 化 乙 烯 / 氧 化 丙 m 水 準 1 調 整 至 氣 凝 膠 製 法 中 所 用 特 定 溶 劑 之 親 水 程 度 K 使 異 氰 酸 1 1 根 端 的 預 聚 合 物 能 溶 於 此 溶 劑 0 若 用 較 多 疏 水 性 溶 劑 (舉 1 例 如 HCFC 22 HFC 134a 二 氧 咸一 氟 甲 烷 液 態 C0 a ) t 1 1 則 有 0 : 100 及 80 :20 間 乙 烯 化. 氧 / 丙 烯 化 氧 水 準 的 疏 水 性 1 I 羥 烧 化 單 酵 或 元 醇 佔 儍 先 7- 例 如 得 卜 内 門 PLC 的 1 1 1 1 1 1 1 1 本紙张尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 經濟部中央標準局員工消費合作社印製 315375 A7 B7 五'發明説明(5)315375 Α7 Β7 The Ministry of Economic Affairs Central Standards Bureau employee consumption cooperation du printing 5. V. Description of the invention (1) The present invention relates to organic aerogels, more specifically to polyisocyanate-based aerogels and their preparation methods. ~ Polyisocyanate-based rigid foam% polyurethane and polyisofluorourate foam, etc. are well known in the art. They are used as thermal insulation media, for example, in the structure of refrigeration equipment. Foams such as & are generally made by reacting suitable polyisocyanates and polyols in the presence of a blowing agent. The thermal insulation properties of rigid foams depend on many factors, including the size of the air cell of the closed rigid foam and the thermal conductivity of the content of the air cell (that is, the blowing agent used in the foam process). One of the substances used in the production of quality polyurethane and polyisocyanurate foams has been widely used as a blowing agent is a fully halogenated atmosphere-containing fluorocarbon, especially trichlorofluoromethane (CFC-11). The very low heat rate of these blowing agents, especially cpc-u, can produce rigid foams with extremely effective thermal insulation. Recent concerns about the potential of chlorofluorocarbons to deplete odors in the atmosphere have led to an urgent need to develop materials that can be changed to environmentally friendly materials, to replace chlorofluorocarbon blowing agents, and to manufacture them for a variety of uses. Foam of the necessary nature. Such other blowing agents technically claimed include hydrofluorocarbons, argon fluorides and (cyclo) alkanes. Although these materials are more environmentally acceptable than CFCs (their ozone depletion potential (ODP) is small or even zero), the heat retention is slightly worse. — In view of the strong demand for energy consumption and environmental legislation, we explored selected polyisocyanate-based insulation materials. One of these options is an evacuated thermal insulation panel filled with open-cell hard polyurethane foam. Vacuum can eliminate the heat conduction of the gas in the sample and reduce the thermal conductivity of the sample. However, the thermal conductivity of this vacuum insulation panel is due to the gas such as air and water vapor inside the panel. This paper size is applicable to the Chinese National Standard (CNS) Α4 specification (210X 297 mm) (please read the note on the back first Please fill in this page again.) 袈.,-* A7 B7 Printed by the Employee Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs. 5. Description of invention (2) It gradually spreads and increases rapidly with the increasing internal pressure over time. Aerogel is known for its super insulation because it excludes any involvement from cypress. These substances are good for the environment because they are full of emptiness. And it is not easy to age. Aerogel is a unique type of open-cell foam with ultra-fine air cell size and low density. #Gel has porosity, and its pore size is lower than the microstructure of the average free channel of air (the pore size is in the common sand range), which is the reason for its abnormal thermal properties. Traditional aerogels are made of inorganic substances (such as silica, alumina or zirconia aerogels) by hydrolysis and condensation of gold fermented salt. Silica gas. Gel has been developed as a super-insulating material such as window glass. Organic aerogels are expected to have lower thermal conductivity, thus providing less heat loss in thermal insulation applications. Recently, organic aerogels have been developed. US Patent Nos. 4997804 and 4873218 illustrate resorcinol-formaldehyde aerogels. U.S. Patent Nos. 5,060,085 and 5,811,163 describe melamine-formaldehyde aerogels and the like. -, Organic aerogels based on polyisocyanate chemistry have never been described before. Therefore, the object of the present invention is to provide an organic aerogel based on polyisocyanate compound and its preparation method. The present invention thus provides a polyisocyanate-based organic aerogel. The term "polyisocyanate-based" used in this article means the aerogel of the present invention can have the following types: polyurethane aerogel, polyurea aerogel * polyisocyanurate aerogel, polyisofluoride Urate / polyurethane aerogel, polyadenylate aerogel, polydicoordinate aerogel, poly || di-adeno aerogel. The aerogel according to the invention has a pore size of less than or equal to 100 nni. Generally, the pore size is in the range of 1 to 100 nm, and more often in the range of 5 to 50 nm. The paper size is applicable to the Chinese National Falcon (CNS) Μ specification (210 X 297 gong) (please read the back side first (Notes to fill out this page) 袈 · Order 315375 A7 _ B7 V. Description of the invention (3) Often in the range of 5 to 25 nm. The pore size can be determined visually by transmission electron microscopy (TEM) or Brunauer-Emmet-Teller nitrogen adsorption (BET) for mercury porosimetry. The quoted pore size value is the average pore diameter measured by the Micromeritics AS # 2000 type 3.0 porosimeter system for root nitrogen liquid adsorption. The average pore diameter is calculated at 4 V / A, where V = cumulative porosity per gram of material and A = specific surface area determined by 5-point BET. The density of the aerogel of the present invention is generally in the range of 1 to 1000 kg / η3, more often in the range of 10 to 800 kg / m3, more often in the range of 20 to 400 kg / n3 or even 30 to 300 kg / m3 or even 90 Up to 200 kg / m3. The density can be determined by weighing and measuring the immersion displacement water capacity, or by weighing and measuring the geometric volume of a sample with a regular shape. The surface area of the pneumatic knee of the present invention is generally in the range of 10 to 1500 m2 / g, more often in the range of 50 to 1200 m2 / g-, more often in the range of 200 to 1000 m2 / g or even 700 to 1000 m2 / g. The surface area can be determined by, for example, BET. The organic polyisocyanate-based aerogel of the present invention can be mixed with a polyisocyanate and an isocyanate trimerization catalyst in an appropriate solvent to keep the mixture in a static state for a long period of time to form a polymerized gel Made of glue. Failed this way-I m In ..... i HI -I--HI In One OJ (please read the precautions on the back and then fill out this page) The Ministry of Economic Affairs Central Standards Bureau employee consumer cooperative prints different and more Plus ground. The sexual roots are rooted in the life of the super-gelatinized acid, and the post-condensation ester cyanide internal gas acid is a different agent. The urinary solubility of the cyanide can be different from the static state. It is suitable for this high one. Even more together. Liang and Shu mixed the modified ester amine to maintain the dry alkanoate to protect urine cyanide. The cyanide polymer paper of the Chinese standard (CNS) A4 specification is suitable for the standard of the cyanide polymer paper which is super-coated with multi-enzymes, analysing the polyalkane, and dissolving polyuria. (210X297mm) A7 B7 The Ministry of Economic Affairs Central Standards Bureau employee consumption cooperation du printed five. Invention description [4 '1 1 I Can 0 The aerogel thus obtained is based on polyurethane and / or polyadeny chemistry 0 this 1 1 1 The alternative manufacturing method allows a larger selection of the dissolved m and increases the gelation time and drying conditions. The content of the treatment can be obtained. 1> 1 1 The polyisocyanate used in this manufacturing method of this aerogel is included in the literature Known for reading 1 I for making poly * isocyanurate materials commonly used for aliphatic cycloaliphatic aryl aliphatic and backside 1 I of 1 aromatic polyisocyanate. Particularly important are aromatic polyisocyanates such as methylbenzene Note 1 I and diphenylmethane diisocyanate week Known Purity, Improvement and Crude Formula Matters 1 1 Re I is especially diphenylmethylene diisocyanate (MDI) or its 2, 4 *-lead 2, 2 'and -4, 4'-isomer formula (passive MD I) and technically known as a crude form of this page. A system made or polymerized MDI (multi-methylene multiple benzene polyisocyanate) with isoacid 1 I a mixture of functionalities greater than 2 and so-called MDI variants (MD I has introduced 1 1 urethane adenylate adenyl biuret N carbodiimide m ketimide 1 I amine or isocyanurate residues and other improvers) 〇Use of gaseous solvents (such as In the case of HCFC 22, the polyisocyanate used in this method for making an aerogel 1 I is preferably a so-called isocyanate-terminated prepolymer made from a reactive compound of polyisocyanate and monoisocyanate. 0 This item is prepared 1 | Isocyanate reactive compounds for prepolymers are preferred Produces a product for the reaction of an alkylene oxide such as ethylene oxide and / or propylene oxide with a monoalcohol or glycol. This hydroxyalkane monoalcohol or binary enzyme has ethylene oxide / propylene oxide m level 1 adjusted to gas condensation The hydrophilicity K of the specific solvent used in the gumming method makes isocyanic acid 1 1 the prepolymer at the root end soluble in this solvent 0 If more hydrophobic solvents are used (for example 1 HCFC 22 HFC 134a dioxin salt monofluoromethane liquid C0 a) t 1 1 has 0: 100 and 80: 20 ethylene. The hydrophobicity of oxygen / propylene oxide level 1 I hydroxy burned mono-enzyme or monohydric alcohol accounted for 7- for example 1 1 of Debne gate PLC 1 1 1 1 1 1 This paper scale is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm) 315375 A7 B7 printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs.

Arlamo卜E 。若用親水性溶劑(舉例如丙酮,2-丁酮)時 刖有20 : 8 0與8 0 : 2 0間ί烯化氧/丙烯化氧水準之親水性 羥烷化單醇或二元醇佔優 在用氫氣化烴或C02作溶劑的特殊情況中本發明方法製 作氣1"凝膠用之多異氰酸酯較佳為自一種多異氰酸酯與一種 ”實質上氟化的異氰酸根反應性化合物”製作之所謂異氰酸 根端基的預聚合物。 此處所用”實質上氟化的異氰酸根反應性化合物”須知係 指至少有-一個異氰酸根反應性官能基其中结合於相應未氟 化的化合物內碳原子之諸氫原子至少有50¾為氟原子置換 的任何有機化合物。 本發明製法中用適當實質上氟化的異氰酸根反應性化合 物為具有式(I)者: *1 [H-Y - (CH2 )m - (Z ' )<, · ]p - A- (Z). - (CHa ) „ - X-H (I) 式内n為自1至11之整數; m係1至1 1 ; P為0或1 ; 一 q為0或1 ; q '為0或1 ; 4 0 0 η I) Υ 係氧,硫,-c-o-式基,或- C- NR ,-S〇2-NR-若 -NR-式基,其中R為氫、CK2烷基或氣化烷 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) m ^im fn^— ·ϋ>— B^l n^i ml tuf ml—Jt (請先閱讀背面之注意事項再填寫本頁) 五、 發明説明( 基; A7 B7 I)Arlamo Bu E. If a hydrophilic solvent (for example, acetone, 2-butanone) is used, a hydrophilic hydroxyalkylated monoalcohol or diol with a level of alkylene oxide / propylene oxide between 20:80 and 80:20 In the special case of using hydrogenated hydrocarbons or CO 2 as a solvent, the polyisocyanate used in the method of the present invention to produce gas 1 " gel is preferably a polyisocyanate and a “substantially fluorinated isocyanate-reactive compound” The so-called isocyanate-terminated prepolymer. The term "substantially fluorinated isocyanate-reactive compound" as used herein means that there is at least one isocyanate-reactive functional group in which the hydrogen atoms bonded to the carbon atoms in the corresponding unfluorinated compound have at least 50¾ Any organic compound replaced by a fluorine atom. The isocyanate-reactive compound suitably fluorinated in the production method of the present invention is of formula (I): * 1 [HY-(CH2) m-(Z ') <, ·] p-A- (Z ).-(CHa) "-XH (I) where n is an integer from 1 to 11; m is 1 to 11; P is 0 or 1; a q is 0 or 1; q 'is 0 or 1; 4 0 0 η I) Υ system oxygen, sulfur, -co-form group, or -C-NR, -S〇2-NR-if-NR-form group, wherein R is hydrogen, CK2 alkyl or gasified alkyl This paper scale is applicable to the Chinese National Standard (CNS) A4 specification (210X297mm) m ^ im fn ^ — · ϋ > — B ^ ln ^ i ml tuf ml—Jt (please read the precautions on the back before filling this page) V. Description of the invention (base; A7 B7 I)

X 係氧,硫,-C-0-式基」或-C-NR so2-hr,-或 -NR'-式基,其中烷基、氟化烷基 、氫或-(CHzU-Uh-A-HZ’h.-WHzU-Y-HU 式基 11X is oxygen, sulfur, -C-0-form group "or -C-NR so2-hr,-or -NR'- group, wherein alkyl, fluorinated alkyl, hydrogen or-(CHzU-Uh-A -HZ'h.-WHzU-Y-HU type base 11

0 II 及Z’ 各獨立為-C-0- ,-C-HR”,或- S〇2-HR”式基,其 中ir係氫0 II and Z ’are each independently -C-0-, -C-HR", or -S〇2-HR "formula, wherein ir is hydrogen

Cl- 1-12 烷基 氣化烷基或 -((:Η2)„-Α-[((:Η2)·-Υ-Η]ρ 式基,或-R”’-Y-H 式 基其中R"'為^-:^亞烷基;又随意 當P係0時A為實質氟化或全氟化的含自2至10碳 原子之直鏈或支鐽烷基;或 當P係1時A為筲質氟化或全Ιί化的含自2至10碳 原子之直鏈或支鍵亞烷基。 本發明方法用一群較佳實質氟化的異氰酸根反應性化合 物為具上述式(I)者,其中X與Υ皆係氧,而A 、Ζ 、 Z’、n 、m 、p 、q及q'有上述任何意義,較佳p為〇 。 本發明方法用特佳實質氟化的異氰酸根反應性化合物為 具式(11)者: — (i ) (ϋ ) n^' t^in mV ^il^i *^ϋ n 111 一OJ (請先閲讀背面之注意事項再填寫本頁) 經濟部中夬標準局員工消費合作杜印製 (CH2)n-〇H / (II) 式内A係實質氟化或全氟化含自2至10碳原子的直鍵或支 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 經濟部中央標隼局員工消費合作社印製 A7 B7 五、發明説明(7 ) 鐽烷基而η為1至11。'特別可提述的式(II)化合物其中η 為1或2 ,Α係全氟C3:。直璉或支鏈烷基如(全氟丙) 基甲醇,(全氟丁基)甲(全氟戊基)甲醇,(全氟 己基)甲醇,(全氟庚基)甲醇,(全氟辛基)甲醇,( 全^壬基)甲醇,(全氟乙基)乙醇,(全氟丙基)乙醇 ,(全氟丁基)乙醇,(全氟戊基)乙醇,(全氣己基) 乙醇,(全氟庚基)乙醇及(全氟辛基)乙醇。 另一特別提述可對式(II)諸化合物,其中η為1或2 , Α係實質-氟化的直鏈或支鏈烷基如1Η,1Η,7Η十二氟-1-庚醇•四氟丙醇,十二氟庚醇,八氟戊醇,十六氟壬醇, 1H· 1H-全氟辛醇,六氟丙醇。 本發明方法用實質氟化異氰酸根反應性化合物之另一特 佳群為具式(III)者: «Η. A-SOz-N- (CH2)n-〇H (III) I!Cl-1-12 alkyl gasification alkyl group or-((: Η2) "-Α-[((: Η2) · -Υ-Η] ρ formula group, or -R" '-YH formula group where R " 'Is ^-: ^ alkylene; optionally when P is 0, A is a substantially fluorinated or perfluorinated linear or branched alkyl group containing from 2 to 10 carbon atoms; or when P is 1 It is a linear or branched alkylene group containing from 2 to 10 carbon atoms, which is fluorinated or fully fluorinated. The method of the present invention uses a group of preferably substantially fluorinated isocyanate-reactive compounds having the above formula (I ), Where X and Υ are both oxygen, and A, Z, Z ', n, m, p, q and q' have any of the above meanings, preferably p is 0. The method of the present invention uses particularly good substantially fluorinated The isocyanate-reactive compound is of formula (11): — (i) (ϋ) n ^ 't ^ in mV ^ il ^ i * ^ ϋ n 111 1 OJ (Please read the precautions on the back before filling in this (Page) Ministry of Economic Affairs China National Bureau of Standards and Staff's consumer cooperation du printing (CH2) n-〇H / (II) formula A series of substantially fluorinated or perfluorinated paper containing 2 to 10 carbon atoms with direct bonds or branched paper The standard is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm). Printed by Zakusha A7 B7. V. Description of the invention (7) Alkyl group and η is 1 to 11. 'In particular, the compound of formula (II) where η is 1 or 2 can be mentioned, and A is perfluoro C3 :. Zhilian Or branched-chain alkyl such as (perfluoropropyl) methanol, (perfluorobutyl) methyl (perfluoropentyl) methanol, (perfluorohexyl) methanol, (perfluoroheptyl) methanol, (perfluorooctyl) Methanol, (per ^ nonyl) methanol, (perfluoroethyl) ethanol, (perfluoropropyl) ethanol, (perfluorobutyl) ethanol, (perfluoropentyl) ethanol, (perfluorohexyl) ethanol, ( Perfluoroheptyl) ethanol and (perfluorooctyl) ethanol. Another special mention can be made to the compounds of formula (II), where η is 1 or 2, Α is substantially fluorinated linear or branched alkyl Such as 1Η, 1Η, 7Ηdodefluoro-1-heptanol • Tetrafluoropropanol, dodecafluoroheptanol, octafluoropentanol, hexafluorononanol, 1H · 1H-perfluorooctanol, hexafluoropropanol The method of the present invention uses another particularly preferred group of substantially fluorinated isocyanate-reactive compounds of formula (III): «Η. A-SOz-N- (CH2) n-〇H (III) I!

Rv 式内A為實質氟化或全氟化的含自2至10碳原子之直鏈或 支鏈烷基* η係1至11 ;及 _ R”為氫或(^-12烷基或R”’-〇H其中R”’係。-^亞烷基。 特別提述式(III)之諸化合物其中η為1或2而A係全氟 Ce-8直鐽或支鏈烷基,R”為氫或烷基或R”’-〇H其中 R”’係Ci-4亞烷基者,如N -乙- N- 2-羥乙替全氟辛烷磺醯 胺,N -甲-N-2-羥乙替全氟辛烷磺醯胺,N -丙- N- 2-羥乙 -10- 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) I vm ^in ti^^i n^i In 1 1 (請先閱讀背面之注意事項再填寫本頁) 315375 Λ7 Β7 經濟部中央標準局員工消费合作社印製 五、發明说明(8) 替全氟辛烷磺醯胺,1Γ-2-羥乙替全氟辛烷磺醸胺,N-乙 -N_2-羥甲替全氟辛烷攝醢-胺,N-甲-H-2-羥甲替全氟辛 烷磺醯胺,N -丙- N- 2-羥^替全氟辛烷磺醯胺,N-2 -羥甲 替全氟辛烷磺醢胺,N-甲-N-2-羥乙替全氣己烷磺醯胺及 雙-為-2-羥乙替全氟辛烷磺醯胺。 實質氟化的異氰酸根反應性化合物(等)可與其反應生 成供本發明製法用的多異氰酸酯組合物之適宜有機多異氰 酸酯包括技術上製備硬聚尿烷或尿烷改良的多異氰尿酸酯 泡沫之任-何已知者•特別為芳族多異氰酸酯如二苯基甲烷 二異擇:酸酯成其2, 4'- ,2, 2’-及4, 4·-異構物與其混合 物式者,二笨基甲烷二異氰酸酯(MDI)及其齊聚物等之混 合物技術上稱作、、粗製"或聚合型M D I (多亞甲基多次苯 基多異氰酸酯)有大於2之異氰酸根官能度者,甲苯二異 氰酸酯成其2,4-及2 ,6-異構物及、其混合物,1,5-萘二異氰 酸酯及1,4-二異氰酸基苯。可提述的其他有機多異氰酸酯 包括脂族二異氰酸酯如異佛爾酮二異氰酸酯,1,6 -二異氰 酸基己烷及4,4'-二異氰酸基二環己基甲烷。 本發明製法中所用異氰酸根终端的預聚合物可由添加一 特別實質氟化的異氰酸根反應性化合物於有機多異氰酸酯_ 或者添加幾種不同實質氟化的異氟酸根反應性化合物之混 合物於有機多異氰酸酯例如在異氰酸根末端的預聚合物製 法之技衡上週知的條件下便利製V備。添加適宜於自50t:至 1 0 0 t:範圍内升溫時將姐份徹底混和,並繼續在升溫混合 Μ迄實質上全部異氰酸根反應性化合物已與有機多異氰酸 -11- 本紙張尺度適用中國國家橾準(CNS ) Α4規格(210 X 297公釐) (請先閱讀背面之注意事項再填寫本頁) 袈· 訂 經濟部中央標準局員工消費合作社印製 A7 B7 五、發明説明(9 ) 酯反應而成。實質氟化的異氰酸根反應性化合物(等)適 當添加蠆在有機多異氰瘡酯重量基之自0.02至30¾ ,較佳 〇 . i至50¾重量比範圍内。.. 為改善本發明製法中所用多異氰酸酯姐合物之穩定性以 使#所得氟化異氰酸根末端預聚合物之脲基甲酸酯變體為 有利。由所得氟化異氰酸根末端預聚合物與有機多異氰酸 酯本身於適當觸媒存在中反應能製備此脲基甲酸酯變體。 改進本發明方法中所用多異氰酸酯姐合物穩定性之另一方 法為使用-由有櫬多異氰酸酯與二種Μ上不同的實質氟化之 異氰酸根反應性化合物的混合物反應得到之所謂混合預聚 合物。亦能用此等混合預聚合物的脲基甲酸酯變體。此等 較佳預聚合物實例包括自Ν -乙- Ν- 2-羥乙替全氟辛烷磺醯 胺與Ν-甲-Ν-2-羥乙替全氟辛烷磺醯胺按變化自1〇:1至 ·» 1:10及較佳自5:5至1:9的比率衍生之預聚合物,自(全 氟己基)(ra)乙酵與Ν-乙-或Ν -甲-Ν-2-羥乙替全氟辛烷 磺醯胺按變化自1 0 : 1至1 :1 0、較佳約1 : 1之比率衍生的預 聚合物。 本發明製法中所用多異氣酸酯成份可僅含一型之該反應 產物或者可含由不同實質氟化的異氰酸根反應性化合物及^ /或不同多異氰酸酯衍生的不同型該反應產物。 本法製備本氣凝膠用的多異氰酸酯用量範圍以總反應混 合物重量基計範圍自0.5至30¾ /重量,較佳自2至20¾重 量,更佳自3至10¾重量。 本製法用較高官能度異氰酸根反應性化合物包括亞垸化 -12- 本紙張尺度適用中國國家樣隼(CNS ) A4規格(210X 297公釐> (請先閲讀背面之注意事項再填寫本頁) 裝· 訂 經濟部中央標準局員工消費合作社印製 A7 ΒΊ___ 五、發明説明(1Q) 氧例如乙烯化氧及/或丙烯化氧,附帶每分子含2至8個 •V. 活性氫原子之引發劑。兩得反應產物宜有平均羥基數自 300至1000,特別自700至-1000 mg KOH/g ,及羥官能度 自2至8 ,特別自3至6 。適宜引發劑包括:多元醇例如 水/甘油,乙二醇,二甘醇,三(羥甲)基丙烷,三(乙 酵)胺,季^四醇,間苯二酚,那苯二酚,花楸糖酵及蔗 糖;多元胺例如乙二胺,甲苯二胺,蜜胺,1,2,3 -三胺基 苯,1,3,4-三胺基苯,二乙撐三胺,四乙撐五胺,五乙撐 六胺,二胺基二苯基甲烷及多亞甲基多次苯基多肢;與胺 基醇例如乙醇胺,二乙酵胺及三乙醇胺;與此等引發劑之 混合物。本製法用較佳較髙官能度異氰酸根反應性化合物 包括羥乙化/羥丙化的乙二胺。如有多官能異氰酸根反應 性化合物存在時|Μ多異氰酸酯量為基礎其用量範圍自1 至60¾ ,較佳自重量比5至30 L。 多異氣酸酯與較高官能度異氰酸根反應性化合物在異氰 酸酯指數於100與600間變動時,較佳於約400之指数反 應。 本製法用之三聚作用觸媒包括技術上所知之任何異氰酸 酯三聚作用觸媒如季銨氫氧化物,鹼金屬與鹼土金屬氫氧L 化物,酵鹽及羥酸鹽如醋酸鉀及2 -乙基己酸鉀,某些叔胺 及非鹼性金羼羥酸鹽如醋酸鉛,及對稱的三畊衍生物等。 特別Μ三畊衍生物為佳。本法用^特佳三聚作用觸媒為得自 A b b 〇 11 L a b 〇 r a t 〇 r i e s 的 Ρ ο 1 y c a t 4 1 及得自 A i r Products之 DABCO TMR, TMR-2與 TMR-4 。 -13- 本紙張尺度適用中國國家樣準(CNS ) A4規格(210X297公釐.) I 1 I— g *l^i m HI i、^OJ (請先閲讀背面之注意事項再填寫本頁) 315375 經濟部中央標準,局員工消費合作社印製 A7 B7 五、發明説明(11 ) 本製法中所用尿烷觸媒包括技術上已知促進尿烷與/或 尿素反應的任何觸媒。i宜尿烷觸媒包括脂族與芳族叔胺 如N,N -二甲替環己胺,有赞.金屬化合物特別錫化合物如辛 酸亞錫及二月桂酸二丁基錫,鹼金羼鹽等。較佳尿烷觸媒 包括<得自卜内門的觸媒SFC 、觸媒SFB二者及得自Un ion Carbide 的 Niax A1 。 能用任何姐合的三聚作用觸媒與尿烷觸媒之混合物。觸 媒包的成分將視所須反應狀況而定。尿烷觸媒/三聚作用 觸媒之重量比變化在0與2:1之間。 多異氰酸酯/缌觸媒重量比率在5與1000之間變動。較 佳多異氰酸酯/觸媒重量比視多異氰酸酯用童、反應/热 化溫度、所用溶劑及所用添加劑(如多官能多元醇等)而 定。 Μ下規則應用作(非包括一切的)實例。在總反應混合 物重量基約2 0¾的多異氰酸酯水準時較佳多異氰酸酯/觸 媒重最比高於600 ,宜在700與800間;在缌反應混合物 基計多異氰酸酯水準約15¾重量時該比率在400與700之 間,較佳500與600間;在總反應混合物基計多異氟酸酯 水準約10¾重量時該比率在350與550間,較佳40 0與__ 5 0 0之間,而在低多異氰酸酯水準(總反應混合物基約 5%重量)時該比率在50與450間,較佳在1〇〇與350之間 。若多異氰酸酯與異氟酸根反懕<性化合物的預聚合物與氣 態溶劑一起使用時約20 vfti:多異氰酸酯之此等較佳多異氰 酸酯/觸媒比率在100與400間變化,約15 wt%多異氟酸 -14- 本纸張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) I------- 參-- (請先.閱讀背面之注意事項再填寫本頁)In the Rv formula, A is a substantially fluorinated or perfluorinated linear or branched alkyl group containing from 2 to 10 carbon atoms * η is 1 to 11; and _ R "is hydrogen or (^ -12 alkyl or R "'-〇H where R"' is.-^ Alkylene. Special reference to compounds of formula (III) where η is 1 or 2 and A is perfluoro Ce-8 straight or branched alkyl, R "Is hydrogen or alkyl or R" '-〇H where R "' is Ci-4 alkylene, such as N-ethyl-N-2-hydroxyethyl substituted perfluorooctane sulfonamide, N-methyl- N-2-hydroxyethyl substituted perfluorooctane sulfonamide, N-propyl-N- 2-hydroxyethyl-10- This paper scale is applicable to China National Standard (CNS) A4 specifications (210X297mm) I vm ^ in ti ^^ in ^ i In 1 1 (Please read the precautions on the back before filling in this page) 315375 Λ7 Β7 Printed by the Employee Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs V. Invention Instructions (8) Substituting PFOS, 1Γ-2-hydroxyethyl substituted perfluorooctane sulfonamide, N-ethyl-N_2-hydroxymethyl substituted perfluorooctane perfluorooctane-amine, N-methyl-H-2-hydroxymethyl substituted perfluorooctane sulfonamide Amine, N-Propyl-N- 2-hydroxy ^ -perfluorooctane sulfonamide, N-2-hydroxymethyl-perfluorooctane sulfonamide, N-methyl-N-2-hydroxyethanidine Alkylamide and bis-is- 2-Hydroxyethyl substituted perfluorooctane sulfonamide. Substantially fluorinated isocyanate-reactive compounds (etc.) can react with them to form suitable organic polyisocyanates including polyisocyanate compositions for use in the process of the present invention. Polyurethane or urethane-modified polyisocyanurate foam-any known one • Especially aromatic polyisocyanates such as diphenylmethane diisoselection: acid ester into its 2, 4'-, 2, 2'- and 4, 4 · -isomers and their mixtures, the mixture of dibenzyl methane diisocyanate (MDI) and its oligomers is technically called, crude " or polymeric MDI (Dorya Methyl multiple phenyl polyisocyanates) with isocyanate functionality greater than 2, toluene diisocyanate into its 2,4- and 2,6-isomers and mixtures thereof, 1,5-naphthalene diisocyanate and 1,4-Diisocyanatobenzene. Other organic polyisocyanates that may be mentioned include aliphatic diisocyanates such as isophorone diisocyanate, 1,6-diisocyanatohexane and 4,4'-diisocyanate Isocyanato dicyclohexylmethane. The isocyanate terminal prepolymer used in the production method of the present invention can be added by adding a special Substantially fluorinated isocyanate-reactive compound in organic polyisocyanate-or adding a mixture of several different fluorinated isofluorate-reactive compounds in organic polyisocyanate, such as a prepolymer at the isocyanate end It is convenient to make V preparation under the conditions known last week. Adding is suitable for thoroughly mixing the sister parts when the temperature is raised from 50t: to 100t: and continues to mix at the temperature. M. Almost all isocyanate-reactive compounds have been added. With organic polyisocyanate-11- This paper scale is applicable to China National Standard (CNS) Α4 specifications (210 X 297 mm) (please read the precautions on the back before filling out this page) 袈 · Order the Central Bureau of Standards of the Ministry of Economic Affairs Employee consumption cooperatives print A7 B7. V. Description of invention (9) Ester reaction. The substantially fluorinated isocyanate-reactive compound (etc.) is suitably added in the weight ratio range of 0.02 to 30¾, preferably 0.1 to 50¾, based on the weight of the organic polyisocyanate ester. .. In order to improve the stability of the polyisocyanate compound used in the production method of the present invention, it is advantageous to make the allophanate variant of the fluorinated isocyanate terminal prepolymer obtained. This allophanate variant can be prepared by reacting the resulting fluorinated isocyanate terminal prepolymer with the organic polyisocyanate itself in the presence of a suitable catalyst. Another method to improve the stability of the polyisocyanate compound used in the method of the present invention is to use the so-called mixed polymer. It is also possible to use these mixed prepolymer allophanate variants. Examples of such preferred prepolymers include from N-ethyl-N- 2-hydroxyethylated perfluorooctane sulfonamide and N-methyl-N-2-hydroxyethylated perfluorooctane sulfonamide. 1〇: 1 to · »1:10 and preferably a prepolymer derived from a ratio of 5: 5 to 1: 9, from (perfluorohexyl) (ra) ethyl yeast and N-B- or N-A- A prepolymer derived from N-2-hydroxyethyl perfluorooctane sulfonamide in a ratio ranging from 10: 1 to 1:10, preferably about 1: 1. The polyisogas ester component used in the production method of the present invention may contain only one type of the reaction product or may contain different types of the reaction product derived from different substantially fluorinated isocyanate-reactive compounds and / or different polyisocyanates. The amount of polyisocyanate used in the preparation of the aerogel in this method ranges from 0.5 to 30¾ / weight based on the total weight of the reaction mixture, preferably from 2 to 20¾ weight, more preferably from 3 to 10¾ weight. This preparation method uses higher-functionality isocyanate-reactive compounds, including sulfonate-12- This paper scale is applicable to the Chinese National Falcon (CNS) A4 specification (210X 297mm> (Please read the precautions on the back before filling in This page) Binding · Order A7 ΒΊ ___ printed by the Staff Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs 5. Description of the invention (1Q) Oxygen such as ethylene oxide and / or propylene oxide, with 2 to 8 per molecule • V. Active hydrogen Atomic initiator. The two-reaction reaction product preferably has an average hydroxyl number from 300 to 1000, especially from 700 to -1000 mg KOH / g, and a hydroxyl functionality from 2 to 8, especially from 3 to 6. Suitable initiators include: Polyols such as water / glycerol, ethylene glycol, diethylene glycol, tris (hydroxymethyl) propane, tris (ethyl yeast) amine, pentaerythritol, resorcinol, naphthophenol, rowan sugar fermentation and Sucrose; polyamines such as ethylenediamine, toluenediamine, melamine, 1,2,3-triaminobenzene, 1,3,4-triaminobenzene, diethylenetriamine, tetraethylenepentamine, Pentaethylenehexamine, diaminodiphenylmethane and polymethylene multiple phenyl multi-limb; with amino alcohols such as ethanolamine, diethylpyramine and tris Alcohol amine; a mixture with these initiators. This method uses preferred isocyanate-reactive compounds with higher functionality including hydroxyethylated / hydroxypropylated ethylenediamine. If polyfunctional isocyanate-reactive compounds are present When | M based on the amount of polyisocyanate, its dosage range is from 1 to 60¾, preferably from 5 to 30 L by weight. Polyisocyanate and higher-functionality isocyanate-reactive compounds have an isocyanate index between 100 and 600 When changing, the index reaction is preferably about 400. The trimerization catalyst used in this method includes any isocyanate trimerization catalyst known in the art such as quaternary ammonium hydroxide, alkali metal and alkaline earth metal hydroxide L compounds , Fermented salt and hydroxy acid salt such as potassium acetate and potassium 2-ethylhexanoate, some tertiary amines and non-alkaline auronic acid hydroxy acid salt such as lead acetate, and symmetrical tri-cultivated derivatives. The best catalyst used in this method is the tri-catalyst catalyst Δ 1 ycat 4 1 from A bb 〇11 L ab 〇rat ries and DABCO TMR, TMR-2 and TMR- from A ir Products 4. -13- This paper scale is applicable to China National Standards (CNS) A4 Specifications (210X297 mm.) I 1 I— g * l ^ im HI i, ^ OJ (please read the precautions on the back before filling this page) 315375 Central Standard of the Ministry of Economic Affairs, printed by A7 B7 by the Bureau ’s Employee Consumer Cooperative V. Description of the invention (11) The urethane catalyst used in this production method includes any catalyst known in the art to promote the reaction of urethane and / or urea. I Urethane catalyst includes aliphatic and aromatic tertiary amines such as N, N- Dimethycyclohexylamine is good. Metal compounds, especially tin compounds, such as stannous octoate and dibutyltin dilaurate, alkali gold and so on. Preferred urethane catalysts include < catalyst SFC, catalyst SFB from Inner Gate, and Niax A1 from Union Carbide. It can use any mixture of trimeric catalyst and urethane catalyst. The composition of the catalyst package will depend on the reaction conditions required. Urethane catalyst / trimerization The weight ratio of catalyst varies between 0 and 2: 1. The weight ratio of polyisocyanate / catalyst varies between 5 and 1000. The preferred polyisocyanate / catalyst weight ratio depends on the use of polyisocyanate, the reaction / heating temperature, the solvent used and the additives used (such as polyfunctional polyol, etc.). The rules under Μ should be used as examples (not everything). The polyisocyanate / catalyst weight ratio at a polyisocyanate level of about 2 0¾ based on the weight of the total reaction mixture is preferably higher than 600, preferably between 700 and 800; this ratio is about 15¾ weight based on the polyisocyanate level of the reaction mixture Between 400 and 700, preferably between 500 and 600; when the total reaction mixture base polyisofluorate level is about 10¾ weight, the ratio is between 350 and 550, preferably between 40 0 and __ 5 0 0 At low polyisocyanate levels (about 5% by weight of the total reaction mixture base), the ratio is between 50 and 450, preferably between 100 and 350. If the prepolymer of the polyisocyanate and the isofluorate-refractory compound is used together with the gaseous solvent about 20 vfti: the preferred polyisocyanate / catalyst ratio for polyisocyanates varies between 100 and 400, about 15 wt % Polyisofluoric acid-14- This paper scale is applicable to the Chinese National Standard (CNS) A4 specification (210X297mm) I ------- see-- (please read the precautions on the back before filling this page) )

*1T 經濟部中央標準局員工消費合作社印裝 A7 B7 五、發明説明(12 ) 酯者在5 0與2 0 0間,約'10 w t ίκ多異氰酸酯者在1 0與1 0 0間 (較佳在3 0與6 0間)。‘-根據本發明製法中須用&溶劑應係單體型(未反應的) 多異氰酸酯Μ及聚合型(已反應的)多異氰酸酯之溶劑。 溶#本領應能形成未反應混合物的均勻溶液及溶解反應產 物或至少阻止反應產物絮凝。溶劑有S Hansen溶解度參數 在10與35 MPa1/2間,較佳在15與30 MPa1/2間,最好在 1 8與2 6 Μ P a 1 / 2間為最適當。此外溶液的臨界壓力及臨界 溫度應儘-可能低俾簡化臨界乾燥步驟。 根據本發明方法所用適宜溶劑包括烴類,二烷基醚,環 狀醚,酮,烷酸烷酯,脂族與環脂族氫氟烴,氫氛氟烴, 氯氟烴,氫氯烴,鹵化芳族化合物及含氣醚類。亦能用此 等化合物之混合物。 適宜烴溶劑包括低脂族或環燁如正戊烷,異戊烷,環戊 院,新戊综,己焼及環己院。 作溶劑用的適宜二烷基_包括有2至6個碳原子的化合 物。作適宜醚之實例可提述二甲醚,甲基乙基醚,二乙醚 ,甲基丙基醚,甲基異丙基醚,乙基丙基醚,乙基異丙基 醚,二丙醚,丙基異丙基醚,二異丙醚,甲基丁基醚,甲_ 基異丁基醚,甲基t-丁基醚,乙基丁基醚,乙基異丁基醚 及乙基t-丁基醚。 適宜環狀醚包括四氫呋喃。* 作溶劑用的適當二烷基酮包括丙酮及甲基乙基嗣。 可作溶劑用之適宜烷酸烷酯包括甲酸甲酯,醋酸甲酯, -15- 本紙張尺j复適用中國國家標準(CNS ) A4規格(210X297公釐) . 訂 (請先閱讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印製 A7 B7 五、發明説明(13) 甲酸乙酯及醋酸乙酯。· 可作溶劑用的適宜氫豪烴類包括低氫氟烷如二氟甲烷, 1,2 -二氟乙烷,1,1,1,4,卜4 -六氟丁烷,五氟乙烷, 1,1,1,2-四氟乙烷,1,1,2 ,2-四氟乙烷,五氟丁烷,四氟 丙#及五氟丙烷。 可作溶劑用之適宜氫氛氟烴包括氛二氟甲烷,1,1-二氯 -2,2,2-三氟乙烷,1,卜二氯-1-氟乙烷,1-氛-1,1-二 氟乙烷,卜氯-2-氟乙烷及1,1,1 ,2-四氟-2-氛乙烷。 可作溶-劑用之適宜氯氟烴包括三氯氟甲烷,二氯二氟甲 烷,三氯三氟乙烷及四氟二氛乙烷。 可作溶劑用的適宜氫氯烴包括卜與2 -氯丙烷及二氛甲烷 〇 適宜鹵化芳族物包括一氮苯與二氛苯。 * #» 可作溶劑用的適宜含氟醚包括雙(三氟甲基)醚,三氟 甲基二氟甲基醚,甲基氟甲基醚.。甲基三氟甲基醚,雙( 二氟甲基)醚,氟甲基二氟甲基醚,甲基二氟甲基醚,雙 (氟甲基)醚,2, 2,2-三氟乙基二氟甲基醚,五氟乙基三 氟甲基_,五氟乙基二氟甲基醚,1,1,2,2-四氟乙基二氟 甲基醚,1,2,2,2-四氟乙基氟甲基醚,1,2,2_三氟乙基;^ 氟甲基醚,1,卜二氟乙基甲基醚,1,1 ,1,3,3,3-六氟丙 -2-基氟甲基醚。 根據本發明的方法所用較佳溶<劑為二氛甲烷,甲基乙基 甲酮,四氫呋喃,一氯苯,三氯氟甲烷(CFC 11),氯二氟 甲烷(HCFC 22) ,1,1,卜三氟-2-氟乙烷(HFC 134a), -16- 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 裝 訂 J, (請先閱讀背面之注意事項再填寫本頁) 315375 A 7 B7 五、發明説明(14 ) 1,卜二氯-卜氟乙烷fHCFC 141b)及其混合物等如HCFC 1 41 b / C F C 11 混合物等 - 另一適宜溶劑為液態二f^ib碳(C〇2 )。液體二氧化碳可 在各種壓力(20 °C時63巴Μ上)及溫度下使用。次或超臨 界i氧化碳亦能作溶劑用。次或超臨界二氧化碳之溶劑本 領能經添加適當改良劑例如髏積比0.1至50¾水準的甲醇 ,乙醇,丙酮,HCFC 22 ,二氛甲烷或前述之任何其他溶 劑調整。 在用液體二氧化碳作溶劑之情況中用由多異氰酸酯與一 氟化的異氰酸根反應性化合物如氟化單元酵或二醇製作之 氟化異氰酸根末端的預聚合物在本氣凝膠製法中作多異$ 酸酯證明有利。 多異氰酸酯、觸媒(等)、溶劑及意較高官能度異氰 酸根反應性化合物僅藉搖通反應器或緩慢播動混合物而-混 合。或者先將多異氰酸酯、溶劑.及隨意較高官能度異氣酸 根反應性化合物混合•然後添加觸媒(等)(以任何 順序)。亦可於膠凝後添加若干觸媒以促進後熟化。'混合 能在室溫或於稍高溫度時完成。 在低沸點溶劑(沸點低於室溫)如HCFC 22之情況中@ 劑於其自己蒸汽壓力或在加壓下加進含多異氰酸酯、 經濟部中央標準局員工消費合作社印聚 (請先閲讀背面之注意事項再填寫本頁) (等)與隨意較高官能度異氟酸根反應性化合物的壓 器内。 然後留置混合物歷一段時間以生成聚合型凝膠。時間其月 間變化自1分鐘至數星期視系統及目標空隙大小與密a -17- 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) B7 B7 經濟部中夬榡準局員工消費合作社印製 Λ、發明説明(15 ) 定。可用自約20TC至約50t,較佳40至451C範圍内溫度。 Μ所用溶劑沸點Μ下約lDt:之溫度為佳。在低沸點溶劑如 HCPC 22之情況中密閉容器内壓力維持於其飽和蒸汽壓或 較高壓力,於較高溫度(較佳30至50Ό範圍内)進行膠凝 反#。在此等升高反應溫度時DABCO TMR為較佳三聚反應 觸媒。 绲合物雖在幾小時内膠凝,經發現使凝膠熟化最少2 4小 時有利於獲得一種在其後加工中易於處理的固體凝膠。能 包含在升.高溫度之後热化週期。 所得凝膠小氣室大小必要超臨界乾燥。液體-蒸汽接觸 面處的大毛细力使凝膠於蒸發脫除溶劑時收縮或破裂。在 超臨界乾燥之情況中不受表面張力越過孔隙,乾氣凝膠遂 保持凝膠的原來形態。 本發明所得氣凝膠之超臨界fg燥包**含放置充滿溶劑的凝 膠於控制溫度的壓力容器内,提高容器壓力至溶劑臨界壓 力Μ上(例如填充氮氣)。在其點時容器加熱至溶劑的臨 界溫度以上。幾小時後緩慢釋放器内壓力同時保持恆溫。 在大氣壓時歷一段冷卻時期後取出容器中氣凝膠。 因乾燥步驟期間收縮之故泡沫密度比其理論值高。 臨界乾燥步驟前凝膠可交換入一更適合超臨界乾燋的 劑例如液體二氧化碳中,可能經由一中間溶劑如丙酮或經 由含改良劑的液體二氧化碳。y 根據本發明的氣凝膠及其製法之儍點為此項溶劑交換步 驟不確實必要。根據水性系统的已知有機與無機氣凝膠往 -18- 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) -------- 裝------訂----- (請先閲讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印製 A7 B7 --—--- 五、發明説明(16) 往需要至少二溶劑交檢步驟方能超臨界乾燥。* 1T A7 B7 printed by the Employees ’Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs V. Description of the invention (12) The esters are between 50 and 200, and the ones with approximately 10wt% polyisocyanate are between 10 and 100 (compare Good between 30 and 60). ‘-The solvent used in the preparation method according to the present invention should be a monomeric (unreacted) polyisocyanate M and a polymerized (reacted) polyisocyanate solvent. The ability of ## should be able to form a homogeneous solution of unreacted mixture and dissolve the reaction product or at least prevent the reaction product from flocculating. Solvents have S Hansen solubility parameters between 10 and 35 MPa1 / 2, preferably between 15 and 30 MPa1 / 2, and most preferably between 18 and 26 MPa 1/2. In addition, the critical pressure and critical temperature of the solution should be kept as low as possible to simplify the critical drying step. Suitable solvents for use in the method of the present invention include hydrocarbons, dialkyl ethers, cyclic ethers, ketones, alkyl alkanoates, aliphatic and cycloaliphatic hydrofluorocarbons, hydrofluorocarbons, chlorofluorocarbons, hydrochlorocarbons Halogenated aromatic compounds and gas-containing ethers. Mixtures of these compounds can also be used. Suitable hydrocarbon solvents include low-aliphatic or cyclopentane such as n-pentane, isopentane, cyclopentan, neopentam, sesame and cyclohexane. Suitable dialkyls for use as solvents include compounds having 2 to 6 carbon atoms. As examples of suitable ethers, mention may be made of dimethyl ether, methyl ethyl ether, diethyl ether, methyl propyl ether, methyl isopropyl ether, ethyl propyl ether, ethyl isopropyl ether, dipropyl ether , Propyl isopropyl ether, diisopropyl ether, methyl butyl ether, methyl isobutyl ether, methyl t-butyl ether, ethyl butyl ether, ethyl isobutyl ether and ethyl t-butyl ether. Suitable cyclic ethers include tetrahydrofuran. * Suitable dialkyl ketones for solvents include acetone and methyl ethyl ether. Suitable alkyl alkanoates that can be used as solvents include methyl formate, methyl acetate, -15- This paper size is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm). Order (please read the notes on the back first Please fill in this page for details) A7 B7 printed by the Employee Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economy V. Description of the invention (13) Ethyl formate and ethyl acetate. · Suitable hydrogen hydrocarbons that can be used as solvents include low hydrofluoroalkanes such as difluoromethane, 1,2-difluoroethane, 1,1,1,4, bu 4-hexafluorobutane, pentafluoroethane , 1,1,1,2-tetrafluoroethane, 1,1,2,2-tetrafluoroethane, pentafluorobutane, tetrafluoropropane # and pentafluoropropane. Suitable hydrofluorocarbons that can be used as solvents include atmospheric difluoromethane, 1,1-dichloro-2,2,2-trifluoroethane, 1, budichloro-1-fluoroethane, 1-ambient- 1,1-difluoroethane, chloro-2-fluoroethane and 1,1,1,2-tetrafluoro-2-fluoroethane. Suitable chlorofluorocarbons that can be used as dissolving agents include trichlorofluoromethane, dichlorodifluoromethane, trichlorotrifluoroethane and tetrafluorodichloroethane. Suitable hydrochlorocarbons that can be used as solvents include Bu and 2-chloropropane and dichloromethane. Suitable halogenated aromatics include mononitrobenzene and dichlorobenzene. * # »Suitable fluorinated ethers that can be used as solvents include bis (trifluoromethyl) ether, trifluoromethyl difluoromethyl ether, methyl fluoromethyl ether. Methyl trifluoromethyl ether, bis (difluoromethyl) ether, fluoromethyl difluoromethyl ether, methyl difluoromethyl ether, bis (fluoromethyl) ether, 2, 2,2-trifluoro Ethyl difluoromethyl ether, pentafluoroethyl trifluoromethyl ether, pentafluoroethyl difluoromethyl ether, 1,1,2,2-tetrafluoroethyl difluoromethyl ether, 1,2, 2,2-tetrafluoroethyl fluoromethyl ether, 1,2,2-trifluoroethyl; ^ fluoromethyl ether, 1, difluoroethyl methyl ether, 1,1,1,3,3 , 3-Hexafluoroprop-2-ylfluoromethyl ether. The preferred solvents used in the method of the present invention are dichloromethane, methyl ethyl ketone, tetrahydrofuran, monochlorobenzene, trichlorofluoromethane (CFC 11), chlorodifluoromethane (HCFC 22), 1, 1. Butrifluoro-2-fluoroethane (HFC 134a), -16- This paper size is applicable to China National Standard (CNS) A4 specification (210X297mm) Binding J, (please read the precautions on the back before filling in this Page) 315375 A 7 B7 5. Description of the invention (14) 1, dichloro-difluoroethane fHCFC 141b) and mixtures thereof such as HCFC 1 41 b / CFC 11 mixtures, etc.-Another suitable solvent is liquid ib carbon (C〇2). Liquid carbon dioxide can be used at various pressures (63 bar M at 20 ° C) and temperatures. Secondary or supercritical carbon dioxide can also be used as a solvent. The solvent power of sub- or supercritical carbon dioxide can be adjusted by adding appropriate modifiers such as methanol, ethanol, acetone, HCFC 22, dichloromethane or any other solvent as mentioned above. In the case of using liquid carbon dioxide as a solvent, a prepolymer of fluorinated isocyanate ends made of a polyisocyanate and a fluorinated isocyanate-reactive compound such as a fluorinated unit enzyme or glycol is used in the present aerogel preparation method Medium made polyisocyanate proved to be advantageous. Polyisocyanates, catalysts (etc.), solvents and higher-functionality isocyanate-reactive compounds are only mixed by shaking the reactor or slowly agitating the mixture. Or first mix polyisocyanate, solvent, and optionally higher-functionality isoxate reactive compound • Then add catalyst (etc.) (in any order). Several catalysts can also be added after gelation to promote post-curing. 'Mixing can be done at room temperature or at a slightly higher temperature. In the case of low-boiling solvents (boiling points below room temperature) such as HCFC 22, @agent is added to its own vapor pressure or under pressure to contain polyisocyanate, printed by the Ministry of Economic Affairs Central Standards Bureau employee consumer cooperative (please read the back first Please pay attention to this page and then fill out this page) (etc.) In the press with optional higher-functionality isoflurate-reactive compounds. The mixture is then left for a period of time to produce a polymeric gel. The time varies from 1 minute to several weeks depending on the size and density of the system and the target gap a -17- This paper scale is applicable to China National Standard (CNS) A4 specifications (210X297 mm) B7 B7 Ministry of Economic Affairs, Central Bureau of Preservation of staff consumption The cooperative prints Λ and invention description (15). It can be used from about 20TC to about 50t, preferably from 40 to 451C. The temperature of the solvent used in M is about 1Dt at the boiling point M: the temperature is better. In the case of low-boiling solvents such as HCPC 22, the pressure in the closed container is maintained at its saturated vapor pressure or higher, and gelation is performed at a higher temperature (preferably in the range of 30 to 50 °). At these elevated reaction temperatures, DABCO TMR is the preferred catalyst for the trimerization reaction. Although the compound gels within a few hours, it has been found that maturing the gel for a minimum of 24 hours is beneficial to obtain a solid gel that is easy to handle in subsequent processing. Can be included in the heating cycle after the high temperature. The size of the small gas chamber of the obtained gel must be supercritically dried. The large capillary force at the liquid-vapour contact surface causes the gel to shrink or break when it evaporates to remove the solvent. In the case of supercritical drying, the surface tension is not exceeded by the pores, and the dry aerogel maintains the original shape of the gel. The supercritical fg drying package of the aerogel obtained in the present invention contains placing a gel filled with a solvent in a temperature-controlled pressure vessel, and raising the pressure of the vessel to the critical pressure M of the solvent (for example, filled with nitrogen). At that point, the container is heated above the critical temperature of the solvent. After a few hours, slowly release the pressure in the device while maintaining a constant temperature. Remove the aerogel from the container after a cooling period at atmospheric pressure. The foam density is higher than its theoretical value due to shrinkage during the drying step. Before the critical drying step, the gel can be exchanged into an agent more suitable for supercritical drying, such as liquid carbon dioxide, possibly through an intermediate solvent such as acetone or through liquid carbon dioxide containing modifiers. y The stupidity of the aerogel according to the present invention and its preparation method is that this solvent exchange step is not really necessary. According to the known organic and inorganic aerogels of the water-based system, the paper size is applicable to the Chinese National Standard (CNS) A4 specification (210X297mm) -------- Installation ------ Order- ---- (Please read the precautions on the back before filling in this page) A7 B7 printed by the employee consumer cooperative of the Central Standards Bureau of the Ministry of Economic Affairs ------ V. Invention Instructions (16) At least two solvent inspection steps are required Only supercritical drying.

—V 如此所得氣凝膠表現最泡大小在100 nmM下之敞泡结樓 ° / 本氣凝膠之可能應用包括但不限於在例如冷凍器與结構 内#絕熱物,觸媒支座,選擇性滲透膜,化學處理色析包 內濾氣器,監偵器,透鏡’太陽能收集器及阻抗匹配裝置 等用途。將來懕用能包括輕質絕熱服裝,耐火建材,高解 析测音器,自動集焦相機,電子與磁學之介電間隔材料, 包裝高價-感溫製品用吸音及吸熱器,Cerenkov偵檢器内用 姐件,高能物理用姐件,或作惰性圍腔熔合靶之零件等。 本氣凝膠碾细時能在抽空絕熱板内作填料用。 超臨界乾燥步驟後能包括一碳化步驟產生一種碳氣凝膠 特別適合在電容器内利用。本發明用以T賁例示範但非限 奮例1 秤已知量的聚合型MDI (得自卜内門的Suprasec DNR) 於一敞口杯。隨後加二氯甲烷,攪拌混合物至得均匀摻混 物(20 wt% Suprasec DNR )。用微公升注射筒添加(得 自 Abbott Laboratories 的)Polycat 41觸媒(多異氰數_ 酯/觸媒重量比200 ),用刮勺攪10秒鐘後開始計時。用 .—振動針热化計追踪黏度升高。用沉浸熱電偶在溶液中央 追踪反應發熱。膠凝時間(黏度V到達其最大上升之一半點 處)為73分鐘,最高反應溫度為29Ϊ:。 所得凝膠經超臨界乾燥。凝膠在小瓶内轉移並在室溫用 "19- 本紙張Λ渡適用中國國家樣準(CNS ) A4規格(210X2M公釐) nn ^^^1 ml nn l^i { n n>^ n (請先聞讀背面之注意事項再填寫本頁) 'va 315375 A7 B7 五、發明説明(17 ) 經濟部中央標準局員工消費合作社印裝 氮氣加壓。達到70巴 <力後含容器的爐溫升至250 1C之溫 度。繼績用氮冲洗凝膠Γ小時,保持壓力與溫度不變。媛 慢釋出容器中壓力至達到衣氣條件,同時保持恆溫。冷卻 期(15分鐘)後取出容器中已乾的氣凝膠。 #得凝膠透明,有橙黃色。所得凝膠之密度為800 kg/m3 。所得凝膠用透射電子顯微術(TEM)及Brunauer-Emmet-Tel ler*氮吸附(BET)測量表現特徵。對氣凝膠的 BET測量顯示比面積15 ra2/g 。TEM照相指出特色大小 5 0 n m (-見圖 1 與 2 )。 實例2 在敞口杯内秤一已知量聚合型MDI (得自卜内門的 Suprasec DNR)。隨後加二氮甲烷,攪拌混合物得均匀摻 混物(10 v/t% Suprasec DHR )。用微公升注射器加得自 Μ Abbott Laboratories 之觸媒 Polycat 41 (多異氰酸醋 / 觸媒重量比400 )。反應在密閉杯内於室溫進行。約8小 時後生成凝膠,任其靜置約24小時。 所得凝膠經超臨界乾燥。轉移凝膠入加壓小瓶中’以液 體C0 2於室溫及90至95巴壓力冲洗30分鐘’在液體C02内 於25至28°C及95巴留置30分鐘,再Μ液體C0,於30¾及— 90至95巴另冲洗30分鐘。升溫至50C而保持壓力不變於 90至95巴。然後Κ起臨界C〇2冲洗凝膠3小時。緩慢(1 小時内)釋出容器中壓力至達大^氣條件而保持丨亙溫。冷卻 期後取出容器中已乾氣凝膠。' 得到白色不透明氣凝膠,密度350 kg/)"3 。對氣凝膠之 (請先閱讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家橾準(CNS ) A4規格(210X297公釐) 經濟部中央榡準局員工消費合作社印袈 A7 B7_____ 五、發明説明(18 ) BET測量發現比面積2l〇 m2/g及脫吸附模式時平均孔徑 18 n m 0 〜 管例3 〆〆 按實例2所述路線製一氣凝膠,惟超臨界乾燥步驟前含 溶交換至丙銅。5日内溶劑交換5次,凝膠由黃色透明 轉為白色不透明。 得到一白色不透明氣凝膠,密度350 kg/m3 。對氣凝膠 之BET測量顯現比面積380 m2/g及脫吸附横式之平均孔徑 2 0 n m 0 -管俐4 反應器内置已知量的聚合型多異氰酸酯(得自ICI之 SUPRASEC X2185)。加二氮甲烷至得到二氛甲烷内3¾重量 多異氮酸酯之摻混物。加得自Air Products之觸媒DABC0 *1 TMR使達到多異氰酸酯/觸媒之重量比50。密閉容器,以 磁性攪拌器攪拌混合物。 置密閉容器於451箱内。1小時後生成固態凝膠。留置 容器於45Ό歷9日。此热化時間後經由幾次添加/除脫周 期以丙_交換二氮甲烷。丙酮液份中不含二氛甲烷後Κ液 體二氧化碳於室溫及90至95巴壓力冲洗試樣30分鐘。留1 試樣暴露在液體二氧化碳中3 0分鐘,然後Κ液體二氧化碳 續冲再30分鐘。提高溫度至50°C同時維持90巴壓力並Μ超 臨界二氧化碳冲洗3小時。如此y冲洗後緩慢釋放至大氣壓 而任試樣冷卻。 - 得到白色不透明氣凝膠,密度140至180 kg/m2 ,比表 -21 - 本紙張尺度適用中國國家標準(CNS ) A4%# ( 210X297公釐) I I I I I I I n 訂 I I.V- (請先閱婧背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印裝 A7 _ i '發明説明(19) 面積900 mz/g:及平均孔徑7.5 nm。 實例5 · 秤重聚合型多異氰酸酯>SUPRASEC X2185得自卜内門) 於壓力容器内。加聚異氰酸酯/觸媒水準50之DABCO TMR (ί#自Air Products)及二氯甲烷Μ至得到3¾重量聚異氟 酸酯在二氯甲烷内之摻混物。封閉容器,攪拌混合物,Μ 靜態放進40-45 t:箱中歷7日,繼Κ 7日之室溫热化時間 〇 加壓下於90巴壓力及25¾溫度交換二氮甲烷成液體二氧 化碳。此溶劑交換後升溫至85Ό而仍維持恆壓。Μ超臨界 二氧化碳沖洗容器30分鐘後緩慢釋放壓力與溫度至週圍狀 況〇 所得不透明氣凝膠有密度200 kg/m3 ,比表面積 ·». 800-850 m2/g及平均孔徑6-8 nm。圖3表現所得氣凝膠碾 成100至200公忽粒子大小之粗粉後熱導率(10 °C時λ值 Μ mW/πΓ Κ計)為壓力(Μ毫巴計)之函数。同一氣凝膠 碾细至1 0 -20公忽粒子大小得到圖4所示的λ對壓力成果 0 管例fi — 自SUPRASEC X2185 (得自ICI )及由甲醇衍生的羥化簞 元醇製得一種預聚合物,有乙烯化氧/丙烯化氧含量 I5/85 ,分子量6〇〇及羥基值9i mg KOH/g 。所得預聚合 物之NC0值為15.8¾ 。 秤重已知量此預聚合物於一設有磁性攪拌器的壓力容器 -22- 本纸張尺度適用中國國家標準(CNS ) A4規格(2IOX297公釐) I * n 11 .^111 I n ^ I I I I I-^ (請先閱讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印裝 A7 B7 五、發明説明(20 ) 。加 Polycat 41 (得自’Ai「 Products)與 HCFC 22 之混合 物(0 . 7 5 m 1觸媒/ 5 0 H C f C 2 2 )於預聚合物Μ迄得到 預聚合物在HCFC 22中之溶液。多異氰酸酯/觸媒比 為20。猛攪混合物20分鐘,室溫中靜置5日。 #化期後加HCFC 22於容器至達40巴之壓力。漸升溫至 1 20 °C並維持最高壓90巴。保持此情況歷30分鐘後漸釋壓 力,同時於所定壓力Μ氮冲洗壓力容器。漸放鬆壓力至大 氣狀況後任試樣冷卻。 所得不透明氣凝膠有密度650 kg/in3及表面積4δ m2/g Ο 啻例7 2 g羥丙化乙二胺及8 g SUPRASEC Χ2185 (得自卜內門 )與9 0 g二氛甲烷混合。此混合物中加0 . 1 m 1之觸媒S F C (得自卜内門)。刺播反應混合物1分鐘後靜置於451。 20小時後加 0.005 ml DABCO TMR (得自 Air Products) Μ 增進後熟化反應。生成均勻的半透明凝膠,用前實例5所 述程序超臨界乾燥。 所得氣凝膠有密度427 kg/πι3及平均孔徑18.5 nra ,比 表面積 266m 2/g。 當例8 重複前實例7所述實驗,用1 g羥丙化乙二胺* 0.075 ml 觸媒 SFC 及 0.025 ml Polycat 41 。 在45 °C歷8小時生成均勻凝膠,任於室溫熟化2曰。 超臨界乾燥透明氣凝膠後得到比表面積445 m2/g,密度 -23- 本紙張尺度適用中國國家標準(CNS ) Α4規格(210Χ297公釐) . 裝 i·ν (請先閱讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作杜印裴 315375 A7 B7 五、發明説明(21 ) 398 kg/m3 及孔徑 10.¾ nm 。—V The aerogel obtained in this way exhibits an open-bubble structure with a maximum bubble size of 100 nmM ° / Possible applications of this aerogel include, but are not limited to, eg in the freezer and structure #insulation, catalyst support, choice Sexual permeable membrane, chemical treatment gas filter in the color analysis package, surveillance detector, lens' solar collector and impedance matching device, etc. Future energy applications include lightweight thermal insulation clothing, refractory building materials, high-resolution sound detectors, autofocus cameras, electronic and magnetic dielectric spacers, sound-absorbing and heat absorbers for packaging high-priced temperature-sensitive products, and Cerenkov detectors Sister parts for internal use, sister parts for high-energy physics, or parts for fusion targets in an inert enclosure. When the aerogel is crushed, it can be used as a filler in the evacuated insulation board. The supercritical drying step can include a carbonization step to produce a carbon aerogel, which is particularly suitable for use in capacitors. The present invention is exemplified by, but not limited to, the T Ben example. Example 1 Weigh a known amount of polymeric MDI (Suprasec DNR from Inner Door) in an open cup. Dichloromethane was then added, and the mixture was stirred until a homogeneous blend (20 wt% Suprasec DNR) was obtained. Polycat 41 catalyst (available from Abbott Laboratories) Polycat 41 (polyisocyanate_ester / catalyst weight ratio 200) was added with a microliter syringe, and the timer was started after stirring for 10 seconds with a spatula. Use the .- Vibrating Needle Thermometer to track the increase in viscosity. Use an immersion thermocouple to track the reaction heat in the center of the solution. The gel time (viscosity V reaches half of its maximum rise) is 73 minutes, and the maximum reaction temperature is 29Ϊ :. The resulting gel was supercritically dried. The gel is transferred in a vial and used at room temperature " 19- This paper is suitable for the Chinese National Standard (CNS) A4 specification (210X2M mm) nn ^^^ 1 ml nn l ^ i {n n > ^ n (Please read the precautions on the back before filling in this page) 'va 315375 A7 B7 V. Description of the invention (17) Printed nitrogen pressurized by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs. After reaching 70 bar < force, the temperature of the furnace containing the container rises to a temperature of 250 1C. Following this, the gel was flushed with nitrogen for Γ hours, keeping the pressure and temperature unchanged. Yuan slowly releases the pressure in the container until it reaches the clothing condition, while maintaining a constant temperature. After the cooling period (15 minutes), remove the dried aerogel from the container. # 得 gel transparent, orange-yellow. The density of the resulting gel was 800 kg / m3. The resulting gel was characterized by transmission electron microscopy (TEM) and Brunauer-Emmet-Tel ler * nitrogen adsorption (BET). BET measurement of the aerogel showed a specific area of 15 ra2 / g. TEM photographs indicate a characteristic size of 50 nm (see Figures 1 and 2). Example 2 A known amount of polymeric MDI (Suprasec DNR from Inner Door) was weighed in an open cup. Subsequently, diazomethane was added, and the mixture was stirred to obtain a uniform blend (10 v / t% Suprasec DHR). Use a microliter syringe to add catalyst Polycat 41 (polyisocyanate / catalyst weight ratio 400) from M Abbott Laboratories. The reaction was carried out in a closed cup at room temperature. After about 8 hours, a gel was formed and allowed to stand for about 24 hours. The resulting gel was supercritically dried. Transfer the gel into a pressurized vial and rinse it with liquid CO 2 at room temperature and 90 to 95 bar pressure for 30 minutes. Leave it in liquid CO 2 at 25 to 28 ° C and 95 bar for 30 minutes, and then liquid CO at 30¾ And-Rinse from 90 to 95 bar for another 30 minutes. Increase the temperature to 50C while keeping the pressure constant at 90 to 95 bar. Then the gel was rinsed for 3 hours from critical CO2. Slowly (within 1 hour) release the pressure in the vessel to atmospheric pressure while maintaining the temperature. After the cooling period, remove the dried aerogel from the container. 'Get a white opaque aerogel with a density of 350 kg /) " 3. For aerogels (please read the precautions on the back before filling out this page) The paper size is applicable to the Chinese National Standard (CNS) A4 (210X297mm). The Central Consumers ’Bureau of the Ministry of Economic Affairs of the People ’s Consumer Cooperative A7 B7_____ 2. Description of the invention (18) BET measurement found that the specific area was 2100 m2 / g and the average pore diameter was 18 nm in desorption mode. 0 ~ Tube Example 3 〆〆 An aerogel was prepared according to the route described in Example 2, except that the supercritical drying step contained Dissolve exchange to copper propyl. The solvent was exchanged 5 times within 5 days, and the gel changed from yellow transparent to white opaque. A white opaque aerogel was obtained with a density of 350 kg / m3. The BET measurement of the aerogel revealed a specific area of 380 m2 / g and an average pore size of the desorption horizontal mode 2 0 n m 0 -Tuan Li 4 The reactor contains a known amount of polymerized polyisocyanate (SUPRASEC X2185 from ICI). Add diazomethane to obtain a 3¾ weight polyisocyanate blend in dichloromethane. The catalyst DABC0 * 1 TMR from Air Products was added to achieve a polyisocyanate / catalyst weight ratio of 50. Close the container and stir the mixture with a magnetic stirrer. Place the sealed container in the 451 box. After 1 hour, a solid gel formed. The container was kept on the 9th of the 45 ° calendar. After this heating time, the diazomethane was exchanged with propylene through several addition / removal cycles. After the acetone solution does not contain dichloromethane, the liquid carbon dioxide is rinsed with carbon dioxide at room temperature and a pressure of 90 to 95 bar for 30 minutes. Leave sample 1 exposed to liquid carbon dioxide for 30 minutes, and then continue to flush with liquid carbon dioxide for another 30 minutes. Raise the temperature to 50 ° C while maintaining a pressure of 90 bar and flush with supercritical carbon dioxide for 3 hours. After this rinsing, slowly release to atmospheric pressure and allow the sample to cool. -Obtained white opaque aerogel with a density of 140 to 180 kg / m2, compared with Table-21-This paper scale is applicable to the Chinese National Standard (CNS) A4% # (210X297mm) IIIIIII n Order I IV- (please read Jing first Note on the back and then fill out this page) A7 _ i 'Invention Description (19) Area 900 mz / g: and average pore diameter 7.5 nm printed by the Employees ’Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs. Example 5 • Weighing polymeric polyisocyanate > SUPRASEC X2185 obtained from Buinmen) in a pressure vessel. Add polyisocyanate / catalyst level 50 DABCO TMR (L # from Air Products) and dichloromethane M to obtain a blend of 32 weight polyisofluorate in dichloromethane. Close the container, stir the mixture, and put it statically in a 40-45 t: box for 7 days, following the 7-day room temperature heating time. ○ Under pressure, exchange diazomethane at 90 bar pressure and 25¾ temperature to liquid carbon dioxide. After this solvent exchange, the temperature was raised to 85 ° while still maintaining a constant pressure. Μ Supercritical carbon dioxide rinses the container after 30 minutes and slowly releases pressure and temperature to the surrounding state. The resulting opaque aerogel has a density of 200 kg / m3, a specific surface area of 800-850 m2 / g and an average pore diameter of 6-8 nm. Figure 3 shows the thermal conductivity (lambda value at 10 ° C λ m MW / πΓ Κ) as a function of pressure (M mbar) after the resulting aerogel is crushed into coarse powder with particle sizes of 100 to 200. The same aerogel was crushed to 1 0 -20 ounces to obtain the particle size to obtain the lambda pressure result shown in Fig. 4 Tube example fi — prepared from SUPRASEC X2185 (available from ICI) and hydroxylated alcohol derived from methanol A prepolymer with an ethylene oxide / propylene oxide content of I5 / 85, a molecular weight of 600, and a hydroxyl value of 9i mg KOH / g. The NC0 value of the resulting prepolymer was 15.8¾. Weigh a known amount of this prepolymer in a pressure vessel equipped with a magnetic stirrer-22- This paper scale is applicable to the Chinese National Standard (CNS) A4 specification (2IOX297mm) I * n 11. ^ 111 I n ^ IIII I- ^ (Please read the precautions on the back before filling out this page) A7 B7 printed by the Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs V. Description of the invention (20). Add a mixture of Polycat 41 (available from 'Ai' Products) and HCFC 22 (0.75 m 1 catalyst / 5 0 HC f C 2 2) to the prepolymer M so far to obtain a solution of the prepolymer in HCFC 22 The polyisocyanate / catalyst ratio is 20. The mixture is vigorously stirred for 20 minutes and allowed to stand at room temperature for 5 days. # After the conversion period, add HCFC 22 to the container to a pressure of 40 bar. Gradually increase the temperature to 1 20 ° C and maintain the maximum Pressure 90 bar. Maintain this condition for 30 minutes and then gradually release the pressure. At the same time, flush the pressure vessel with nitrogen at the specified pressure. Gradually relax the pressure to atmospheric conditions and let the sample cool. The resulting opaque aerogel has a density of 650 kg / in3 and a surface area of 4δ m2 / g Ο Example 7 2 g of hydroxypropylated ethylenediamine and 8 g of SUPRASEC Χ2185 (obtained from Bu Nemen) were mixed with 90 g of dichloromethane. To this mixture was added 0.1 m 1 of catalyst SFC ( (Obtained from Bu Neimen). The reaction mixture was stabbed for 1 minute and then stood at 451. After 20 hours, 0.005 ml of DABCO TMR (from Air Products) was added to increase the post-maturation reaction. A uniform translucent gel was generated, using the previous example 5. Supercritical drying according to the procedure described in 5. The obtained aerogel has a density of 427 kg / πι3 and an average pore diameter of 18.5 nra, The surface area is 266m 2 / g. When Example 8 repeats the experiment described in the previous Example 7, using 1 g of hydroxypropylated ethylenediamine * 0.075 ml of catalyst SFC and 0.025 ml of Polycat 41. A uniform gel was generated at 45 ° C for 8 hours, Allow to mature at room temperature for 2 days. After supercritical drying of the transparent aerogel, the specific surface area is 445 m2 / g, and the density is -23. This paper scale is applicable to the Chinese National Standard (CNS) Α4 specification (210Χ297 mm). Install i · ν (Please read the precautions on the back before filling in this page) Employee Consumer Cooperation of the Central Bureau of Standards of the Ministry of Economy Du Yinpei 315375 A7 B7 V. Description of the invention (21) 398 kg / m3 and pore size 10.¾ nm.

•"V 當例9 重複賁例8僅用0.075心觸媒SFC作觸媒。於45 °C歷4 小時後另加0.025 ml DABCO TMR。在45°C1小時後得均勻 固¥凝膠。• " V When Example 9 is repeated, Example 8 uses only 0.075 cardiac catalyst SFC as the catalyst. Add 0.025 ml DABCO TMR after 4 hours at 45 ° C. After 1 hour at 45 ° C, the gel is evenly cured.

苜例1CL 0,6 g經丙化乙二胺、97 g二氛甲烷與2.4 g SUPRASEC X2 185(得自卜内門)在一壓力容器内混合。其中加0.3 ml 觸媒SFC-(得自卜内門)。封閉容器,加熱至45t:歷2小 時。反應混合物中加0.03 ml DABCO TMR (得自AirAlfalfa Example 1CL 0,6 g of propylenediamine, 97 g of dichloromethane and 2.4 g of SUPRASEC X2 185 (from Inner Door) were mixed in a pressure vessel. Add 0.3 ml of catalyst SFC- (obtained from Bu Nemen). Close the container and heat to 45t: 2 hours. Add 0.03 ml of DABCO TMR (available from Air

Products)於反應混合物。90分鐘後生成固體不透明凝膠 0 啻例1 1Products) in the reaction mixture. After 90 minutes, a solid opaque gel was formed. 0 Example 1 1

A 用0.3 g羥丙化乙二胺與2.?、g SUPRASEC X2185重複實 例1 0。 24小時後生成固體不透明氣凝膠。 音例12 製一 10 wU SUPRASEC X2185之甲基乙基甲_溶液。以 多異氰酸酯/觸媒比率300加DABC0TMR (得自Air Products) ° 24小時後生成白色凝膠。將此凝膠於90巴及 室溫作液體二氧化碳溶劑交換,然後超臨界脫除二氧化碳 4 〇 所得氣凝膠有密度90 kg /m3及比表面積56 m2/g 。此氣 凝膠有粉狀结構,平均空隙孔徑(經BET測得)16.7 nra 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (請先閱讀背面之注意事項再填寫本頁) 裝. 訂 五、發明説明(22) A7 B7 經濟部中央標準局員工消费合作社印製 窗例1 3 在四氫呋喃作溶劑中重複實例12,用多異氰酸酯/觸媒 比率 100 之 Polycat 41。 4得氣凝 膠有密度175 kg/n3及比表面積448 m2/g ° g例1 4 在單氣苯作溶劑内重複實例13。反應情況慢,4δ小時後 生成半透明凝膠。 所得氣凝膠有密度284 kg/m3 ,比表面積398 m2/g及孔 徑 1 0 . 2 n m 。 實 溶 4g SUPRASEC X2185於 96 g THF中。加 0.8 g Polycat 41於此混合物。攪拌混合物並留置靜態Μ迄獲溶 九*· 膠-凝膠。交換溶膠-凝膠之溶劑為液體C02 ,然後於 32¾ K上溫度及73巴以上壓力趋臨界乾燥。得一不透明氣 凝膠,密度70 kg/m3,比表面積515 m2/g及平均孔徑1〇 n is ° 窗俐1 fi 溶3 s XR159 (得自卜內門)於125 g CH2CU。此混合 物内加3.6 g SUPRASEC X218 5'(得自卜内門),攪拌混合 物5分鐘後靜態留置室溫Ψ。幾日後形成半透明溶膠-凝 膠。轉移此凝膠至一壓力容器’其中溶劑交換CH2C12為液 體二氧化碳。完全溶劑交換後在32 t:M上溫度及73巴以上 壓力超臨界乾燥溶膠-凝膠,遂成半透明氣凝膠。氣凝膠 -25- 本紙張尺度適用中國國家樣準(CNS ) Α4規格(210Χ:297公釐) (請先閲讀背面之注意事項再填寫本頁) 裝· 、*τ A7 B7 315375 五、發明説明p ) 密度為350 kg/m3 ,比表面積110 m2/g。 置例1 7 ~ 加料20 g SUPRASEC X2185 (得自卜內門)於壓力容器 。沖氮罩後密閉容器,置0.04 ml Polycat P41於反應器 之&射環内。在蒸汽壓力下加料13.6 g (:〇2入反應器,同 時移空注射環。攪拌混合物30分鐘,然後留置反應器在室 溫中靜態歷1日。 此热化時間後加70 g C〇2入鼦力器,升溫至C02的超臨 界溫度(-32Ό)以上。容許器内壓力漸增並保持不變歷至 少30分鐘。然後在恆溫漸釋放器中壓力。壓力容器内部已 達大氣條件後放冷容器至室溫。 得到固體不透明微孔物質,密度280 kg/m3 。 苜例1 8 •I.· 重複實例5用SUPRASEC X24?4 (得自3M之1¾重量 Fluorad FC10與99¾ 重量得自 ICI PLC 之 SUPRASEC X2185 )取代 SUPRASEC X2185。 (Pluorad 係 3M之商標) 生成不透明溶膠-凝膠,超臨界乾烽後產生不透明氣凝 膠,密度183 kg/m3 ,比表面積802 m2/g及平均孔徑9.6 nm ° __ SLM..L9. 重複實例5用1¾重量得i3M的1H,1H,7H-十二氟-1-庚 烷醇及99¾重量得自ICI PLC的^UPRASEC X2273之反應產 物替代 SUPRASEC X2185 。 生成不透明溶膠-凝膠經超臨界乾燥後產生不透明氣凝 -26- 本紙張尺度適用中國國家標準(CNS ) A4規格(2丨0><297公釐) 裝 i I I I J 各 (請先閱讀背面之注意事項再填寫本頁) 經濟部中央標準局員工消費合作社印裝 315375 ay B7 丛、發明説明(>4) P有密度1 7 4 k g / m 3 ,比表面積8 3 6 m 2 / g及乎均孔徑9 . 1 明 說 要 0 圖 為為 1 2 圖圖 之之 膠 0 凝_凝 氣氣 明明 發發 本本 示示 顯顯 Η :1Γ 照照 小小 大大 徵徵 特特 之之 數數 函函 之之 力力 壓壓 為為 性性 電電 導導 熱熱 之之 膠膠 凝凝 氣氧 碾 0 粗碾 明明 發發 本本 示示 顯顙 3 4 圖圖 (請先閲讀背面之注意事項再填寫本頁) 裝.A Repeat Example 10 with 0.3 g hydroxypropylated ethylenediamine and 2.?, G SUPRASEC X2185. After 24 hours, a solid opaque aerogel formed. Example 12 Make a 10 wU SUPRASEC X2185 methyl ethyl methyl solution. A white gel formed after 24 hours at a polyisocyanate / catalyst ratio of 300 plus DABC0TMR (available from Air Products) °. This gel was subjected to liquid carbon dioxide solvent exchange at 90 bar and room temperature, and then supercritical carbon dioxide was removed. The aerogel obtained had a density of 90 kg / m3 and a specific surface area of 56 m2 / g. This aerogel has a powder structure and an average pore size (measured by BET) of 16.7 nra. The paper size is applicable to the Chinese National Standard (CNS) A4 specification (210X297mm) (please read the precautions on the back before filling this page) Binding. Order V. Description of Invention (22) A7 B7 Example of window printing by the Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs 1 3 Repeat Example 12 in tetrahydrofuran as the solvent, using Polycat 41 with a polyisocyanate / catalyst ratio of 100. 4 The obtained gas gel has a density of 175 kg / n3 and a specific surface area of 448 m2 / g ° g. Example 1 4 Example 13 was repeated in a single gas benzene as solvent. The reaction was slow and a translucent gel was formed after 4δ hours. The obtained aerogel had a density of 284 kg / m3, a specific surface area of 398 m2 / g and a pore diameter of 10.2 n m. Solute 4g SUPRASEC X2185 in 96g THF. Add 0.8 g Polycat 41 to this mixture. Stir the mixture and leave the static Μ9 * · gel-gel. The solvent for exchanging the sol-gel is liquid CO2, and then it dries to a critical temperature at a temperature of 32¾ K and a pressure above 73 bar. An opaque aerogel was obtained with a density of 70 kg / m3, a specific surface area of 515 m2 / g and an average pore size of 10 n is ° Window Li 1 fi dissolved in 3 s XR159 (from Inner Gate) in 125 g CH2CU. To this mixture was added 3.6 g of SUPRASEC X218 5 '(from Inner Gate), and after stirring the mixture for 5 minutes, it was left at room temperature Ψ statically. A few days later, a translucent sol-gel was formed. Transfer this gel to a pressure vessel where the solvent exchange CH2C12 is liquid carbon dioxide. After complete solvent exchange, the sol-gel is supercritically dried at a temperature of 32 t: M and a pressure of more than 73 bar to form a translucent aerogel. Aerogel-25- This paper scale is applicable to China National Standards (CNS) Α4 specification (210Χ: 297mm) (please read the precautions on the back before filling in this page). ** A7 B7 315375 V. Invention Note p) The density is 350 kg / m3 and the specific surface area is 110 m2 / g. Example 1 7 ~ Add 20 g SUPRASEC X2185 (from the inner door) to the pressure vessel. Close the container after flushing the nitrogen hood, and place 0.04 ml Polycat P41 in the & injection ring of the reactor. Charge 13.6 g (: 〇2 into the reactor under steam pressure while evacuating the injection ring. Stir the mixture for 30 minutes, then leave the reactor at room temperature for 1 day. Add 70 g C〇2 after this heating time Enter the manpower device and raise the temperature to above the supercritical temperature (-32Ό) of C02. Allow the pressure inside the device to gradually increase and remain unchanged for at least 30 minutes. Then pressurize in the constant temperature gradual release device. Let the container cool to room temperature. Obtain a solid opaque microporous material with a density of 280 kg / m3. Alfalfa Example 1 8 • I. · Repeat Example 5 with SUPRASEC X24? 4 (1¾ weight from 3M Fluorad FC10 and 99¾ weight from ICI PLC's SUPRASEC X2185) replaces SUPRASEC X2185. (Pluorad is a trademark of 3M) Produces opaque sol-gel, opaque aerogel after supercritical drying, density 183 kg / m3, specific surface area 802 m2 / g and average pore diameter 9.6 nm ° __ SLM..L9. Repeat Example 5 to replace SUPRASEC X2185 with the reaction product of 1¾ weight of 1H, 1H, 7H-dodecyl-1-heptanol from i3M and 99¾ weight of ^ UPRASEC X2273 from ICI PLC 。Produce opaque sol-gel super-pro Opaque gas condensation after drying -26- This paper scale is applicable to the Chinese National Standard (CNS) A4 specification (2 丨 0 > < 297mm) Packed with i IIIJ (please read the precautions on the back before filling this page) Printed 315375 ay B7 clumps, invention description (> 4) P with density of 174 kg / m 3, specific surface area of 8 3 6 m 2 / g and average pore diameter of 9. 1 To 0, the picture is the glue of the 1 2 picture. 0 凝 _ 凝气 气 明明 发 发 本 This display shows Η: 1Γ According to the number of small and large numbers, the force of the function of the number is the pressure It is a gel of gel, gel, gas and oxygen for sexual conductivity, heat conduction, and heat. 0 Rough milling. This book shows the display. 3 4 Figures (please read the precautions on the back before filling this page).

、ST 經濟部中央標準局員工消費合作社印製 7 2 本紙張尺度適用中國國家襟準(CNS ) Α4規格(210 X 297公釐), Printed by the Staff Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs 7 2 This paper standard applies to China National Standard (CNS) Α4 specification (210 X 297 mm)

Claims (1)

中文申言 6013號專利申請案 :申11¾利範圍修正本⑽年β月) Α8 Β8 C8 DS 3 補充 經濟部中央標準局^工消費合作社印裝 六、申請專利範圍 1. 一種製備Μ聚異氰酸酯為主的有機氣凝膠之方法,該氣 凝膠具孔徑小於或等於100 nm,密度在1至1000 kg/m3範圍内,及表面積在10至1500 m2/g範圍内,其 包括下列步驟: (a) 將有機聚異氰酸酯與選自由第四銨氫氧化物、鹼金 屬及鹼土金鼷氫氧化物、醇鹽及羧酸鹽、第四胺、 非鹼性金屬羧酸鹽及三畊衍生物所姐成之群之異氰 酸酯三聚作用觸媒混合於選自由烴、二烷醚、環族 醚、_、烷酸烷酯、脂族及環脂族烴、氫氯氟碳化 物、氛氟碳化物、氫氯碳化物、鹵化芳族化合物及 含氟醚所組成之群之溶劑中,其中有機聚異氰酸酯 係二苯基甲烷二異氰酸酯或聚亞甲基聚伸笨基聚異 氰酸酯或異氰酸酯末端的預聚合物,及其用量為基 於總反應混合物之0.5至30¾ Μ重量計,且聚異氰 酸酯/觸媒重量比在5與1 〇 〇 0之間, (b) 將該混合物維持於靜態1分鐘至數週Κ生成聚合型 凝膠,及 (c )超臨界地乾燥所得凝膠。 2. 根撺申請專利範圍第1項之方法,其中較高官能度的異 氰酸酯反應性化合物與尿烷觸媒在(a)步驟中與其他組 份一起混合。 3. 根據申請專利範圍第2項之方法,其中較高官能度的異 氰酸酯反應性化合物為伸烷氧化物與每分子含2至8個 活性氫原子的引發劑之反應產物。 本紙張尺度適用中國國家橾率(CNS)八4規格(210X297公釐) (請先閲讀背面之注意事項再填寫本頁) --------------:袭------ίτ------Τ--- 六、申請專利範園 4. 根據申請專利範圍第3項之方法’其中引發劑為乙二胺 --- - - - ϋ n - - - - - ^ (請先閲讀背面之注意事項再填寫本頁) 0 5. 根撺申請專利範圔第2項之方法’其中高官能度異氰酸 酉兽反應性化合物用量以聚異氰酸醋為基礎在1與60%重 量間變化。 6. 根撺申請專利範圍第1項之方法’其中異氰酸酯三聚作 用觸媒為三哄衍生物。 7. 根據申請專利範圍第2項之方法’其中尿烷觸媒為三級 胺。 _ 8. 根撺申請專利範圍第1項之方法,其中溶劑為二氯甲烷 0 9 · 根據申請專利範圍第1項之方法,其中溶劑經交換後超 臨界乾燥凝膠。 10.根撺申請專利範圍第9項之方法,其中溶劑羥交換成液 體二氧化碳。 U·—種Μ聚異氰酸酯為主的有機氣凝膠,其係根據申請專 利範圍第1項之方法製備,其具孔徑小於或等於1〇〇 n m ,密度在1至1000 kg/m3範圍內,及表面積在10至 15 00 m2/g範圍內。 經濟部中央標準局t工消費合作社印«. 1 2 .根撺申請專利範圍第1丨項之氣凝膠,其孔徑在5至5〇 n m範圍内。 13. 根撺申請專利範圍第u項之氣凝膠,其密度在2〇至4〇〇 kg/m3範圍内。 14. 根據申請專利範圍第u項之氣凝膠,其表面積在2〇〇至 -2 - 本紙張尺度適用中國囷家標準(CNS > A4^ ( 210X297公羞)----Chinese Shenyan Patent Application No. 6013: Application 11 ¾ Amendment Scope (year β month) Α8 Β8 C8 DS 3 Supplement to the Central Bureau of Standards of the Ministry of Economy ^ Printed by the Industrial and Consumer Cooperatives VI. Patent Scope 1. A preparation of polyisocyanate is The main method of organic aerogel. The aerogel has a pore size less than or equal to 100 nm, a density in the range of 1 to 1000 kg / m3, and a surface area in the range of 10 to 1500 m2 / g. It includes the following steps: ( a) The organic polyisocyanate is selected from the group consisting of fourth ammonium hydroxide, alkali metal and alkaline earth gold hydroxide, alkoxide and carboxylate, fourth amine, non-alkaline metal carboxylate and tri-growth derivatives The sister isocyanate trimerization catalyst is mixed with hydrocarbons, dialkyl ethers, cyclic ethers, _, alkyl alkanoates, aliphatic and cycloaliphatic hydrocarbons, hydrochlorofluorocarbons, chlorofluorocarbons , Hydrochlorocarbons, halogenated aromatic compounds and fluoroethers in the group of solvents, of which organic polyisocyanate is diphenylmethane diisocyanate or polymethylene polybenzyl polyisocyanate or isocyanate terminal prepolymerization Substance and its dosage Based on 0.5 to 30¾ MW weight of the total reaction mixture, and the polyisocyanate / catalyst weight ratio is between 5 and 1000, (b) The mixture is kept static for 1 minute to several weeks to form a polymerized gel , And (c) supercritically drying the resulting gel. 2. The method according to item 1 of the patent application scope, in which a higher-functionality isocyanate-reactive compound and a urethane catalyst are mixed with other components in step (a). 3. The method according to item 2 of the patent application scope, wherein the higher-functionality isocyanate-reactive compound is the reaction product of an alkylene oxide and an initiator containing 2 to 8 active hydrogen atoms per molecule. This paper scale is applicable to China National Standard (CNS) 84 specifications (210X297mm) (please read the precautions on the back before filling this page) --------------: 袭- ---- ίτ ------ Τ --- 6. The patent application garden 4. According to the method of item 3 of the patent application scope, where the initiator is ethylenediamine ------ϋ n-- ---^ (Please read the precautions on the back before filling in this page) 0 5. Root out the method of applying for patent patent item No. 2 'where the amount of high-functionality isocyanate unitary reactive compound is polyisocyanate Vinegar based varies between 1 and 60% by weight. 6. The method of the first item in the scope of patent application, where the isocyanate trimerization catalyst is a trident derivative. 7. According to the method of item 2 of the patent application scope, where the urethane catalyst is a tertiary amine. _ 8. The method according to item 1 of the patent application scope, in which the solvent is methylene chloride 0 9 · According to the method in item 1 of the patent application scope, in which the solvent is supercritically dried after the exchange of the gel. 10. The method according to item 9 of the patent application scope, in which the solvent hydroxyl is exchanged into liquid carbon dioxide. U · —an organic aerogel based on Μ polyisocyanate, which is prepared according to the method of item 1 of the patent application, has a pore size of less than or equal to 100 nm, and a density in the range of 1 to 1000 kg / m3, And the surface area is in the range of 10 to 15 00 m2 / g. Printed by the Ministry of Economic Affairs Central Bureau of Standards and Industry Cooperative Co., Ltd. 1 2. The aerogel according to item 1 of the patent application scope has a pore size in the range of 5 to 50 nm. 13. The aerogel according to the patent application scope of U.S.A. has a density in the range of 20 to 400 kg / m3. 14. According to the aerogel of the patent application scope item u, its surface area is between 200 and -2-This paper scale is applicable to the Chinese standard (CNS > A4 ^ (210X297 公 親) ---- …垆利卿,吟却5:ί:ίί參參蜗鱗知―乂 315375 1 000 m2/g範圍内。 經濟部中央標準局員_工消費合作社印製… Yao Liqing, Yin Ke 5: ί: ί ginseng knows snail scales-315375 1 000 m2 / g. Member of the Central Standards Bureau of the Ministry of Economic Affairs (請先閱讀背面之注意事項再填寫本I) 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 六、申請專利範圍 裝. 訂 V'(Please read the precautions on the back before filling in this I) This paper scale is applicable to the Chinese National Standard (CNS) A4 specification (210X297mm). Six, the scope of patent application. Binding V '
TW83106013A 1993-07-22 1994-07-01 TW315375B (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GB939315198A GB9315198D0 (en) 1993-07-22 1993-07-22 Organic aerogels
GB939319451A GB9319451D0 (en) 1993-09-21 1993-09-21 Organic aerogels
GB9412894A GB9412894D0 (en) 1993-07-22 1994-06-27 Organic aerogels

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