CN1048696C - 干凝胶,其制备方法和用途 - Google Patents

干凝胶,其制备方法和用途 Download PDF

Info

Publication number
CN1048696C
CN1048696C CN95108111A CN95108111A CN1048696C CN 1048696 C CN1048696 C CN 1048696C CN 95108111 A CN95108111 A CN 95108111A CN 95108111 A CN95108111 A CN 95108111A CN 1048696 C CN1048696 C CN 1048696C
Authority
CN
China
Prior art keywords
gel
water
organic solvent
gained
sio
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
CN95108111A
Other languages
English (en)
Other versions
CN1124229A (zh
Inventor
R-M·简森
A·兹莫曼
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Aventis Research and Technologies GmbH and Co KG
Cabot Corp
Original Assignee
Cabot Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Cabot Corp filed Critical Cabot Corp
Publication of CN1124229A publication Critical patent/CN1124229A/zh
Application granted granted Critical
Publication of CN1048696C publication Critical patent/CN1048696C/zh
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B33/00Silicon; Compounds thereof
    • C01B33/113Silicon oxides; Hydrates thereof
    • C01B33/12Silica; Hydrates thereof, e.g. lepidoic silicic acid
    • C01B33/14Colloidal silica, e.g. dispersions, gels, sols
    • C01B33/152Preparation of hydrogels
    • C01B33/154Preparation of hydrogels by acidic treatment of aqueous silicate solutions
    • C01B33/1543Preparation of hydrogels by acidic treatment of aqueous silicate solutions using ion exchangers
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B33/00Silicon; Compounds thereof
    • C01B33/113Silicon oxides; Hydrates thereof
    • C01B33/12Silica; Hydrates thereof, e.g. lepidoic silicic acid
    • C01B33/14Colloidal silica, e.g. dispersions, gels, sols
    • C01B33/152Preparation of hydrogels
    • C01B33/154Preparation of hydrogels by acidic treatment of aqueous silicate solutions
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B30/00Compositions for artificial stone, not containing binders

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Silicon Compounds (AREA)
  • Thermal Insulation (AREA)

Abstract

本发明涉及改性SiO2凝胶(干凝胶),其制备和作为绝热材料的用途。这样制备该干凝胶:酸化水玻璃水溶液,加入碱使由此产生的硅酸缩聚为SiO2凝胶,用与水形成冷却时分为两相的共沸物的有机溶剂萃取蒸馏,从形成的凝胶中除去水,该凝胶与甲硅烷基化试剂反应,在低于除水所用有机溶剂的临界压力和/或临界温度的压力和温度下干燥此凝胶。

Description

干凝胶,其制备方法和用途
本发明涉及改性SiO2凝胶(以下称为“干凝胶”)的制备方法,按此方法制得的干凝胶本身和其用途。
经干燥适当的凝胶制备广义上的气凝胶,即“用空气作为分散介质的凝胶”。在此意义上的“气凝胶”包括狭义的气凝胶,干凝胶和低温凝胶。与此相关,当在临界温度以上从临界压力以上的压力开始很彻底地去除凝胶的液体时,干燥的凝胶称为狭义的气凝胶。另一方面,如果在亚临界条件下去除凝胶的液体,例如形成液气界相,形成的凝胶称为干凝胶。
制得的干凝胶与常规SiO2气凝胶相关,但与之不完全相同。
已知SiO2气凝胶具有极好的绝热作用,它们例如通过原硅酸四乙酯在乙醇中酸水解来制备。水解生成凝胶的结构由温度、PH和胶凝过程的持续时间决定。但一般湿凝胶干燥时凝胶的结构崩解,因为在干燥过程中产生的毛细管力极大。在溶剂的临界温度和临界压力以上进行干燥时,可防止凝胶的崩解。因为在此区域液/气相界消失,也不产生毛细管力,在干燥过程中凝胶无变化,即在干燥过程中凝胶也不收缩。基于此干燥技术的制备方法例如公开在EP-A-0396 076或WO92 03378中。但如使用乙醇时此技术要求温度高于240℃,压力大于40巴。虽然在干燥前用CO2代替乙醇,可将干燥温度降至约40℃,但需要80巴的压力。
现发现,当在干燥前与甲硅烷基化试剂反应时,可在亚临界条件下干燥SiO2凝胶。以下将生成的产物称为“干凝胶”。它们是极佳的绝热材料。
本发明涉及干凝胶的制备方法,其包括:
a)用酸性离子交换树脂或无机酸调节水玻璃水溶液至PH≤3.0,优选≤2.2,
b)加入碱,使由此产生的硅酸缩聚为SiO2凝胶,如果a)步中使用了无机酸,需要时用水洗涤凝胶,直至无电解质为止,
c)用与水形成冷却时分离成两相的共沸物的有机溶剂进行萃取蒸馏,从b)步所得凝胶中除去水,直至凝胶的含水量≤5%(重量),
d)c)步所得凝胶与甲硅烷基化试剂反应,
e)在低于c)步所用有机溶剂的临界压力和/或临界温度的压力和温度下干燥d)步所得甲硅烷基化凝胶。
在a)中优选使用的特别适合于此目的的酸性离子交换树脂为含磺酸基的那些。如果使用无机酸,盐酸和硫酸特别适合。水玻璃一般使用钠和/或钾水玻璃。水玻璃的浓度优选在1-20%(重量)范围内,最优选在5-12%(重量)范围内。
在b)步优选使用的碱为NH4OH、NaOH、KOH、Al(OH)3和/或胶态硅酸。如果a)步使用无机酸,用碱产生的SiO2凝胶适当时用水洗涤,直到无电解质为止;最好持续洗涤直到流出的洗涤水与去离子水的电导率相等。
在c)步前,优选使凝胶在一般0-150℃,优选80-130℃,PH4-11,优选4-9条件下老化。老化时间一般为10秒到48小时,优选为10秒到5小时。
在c)步,用有机溶剂萃取蒸馏除去凝胶中所含水,直至凝胶中含水量不超过5%(重量),优选≤2%(重量)。所用溶剂必须与水形成共沸物,冷却时该共沸物分成两液相,水相和溶剂相。适当溶剂的实例为甲苯、二正丁基醚或甲基异丁基酮。优选使用甲苯。
共沸物冷却时形成的溶剂相可再返回此工艺中。
a)到c)步一般在溶液的凝固点到溶剂的沸点间的温度下进行。
在d)步,含溶剂凝胶与甲硅烷基化试剂反应。所用甲硅烷基化试剂一般为式R1 4-nSiCln或R1 4-nSi(OR2)n的甲硅烷,其中n=1-3,R1和R2相互独立地为C1-C6-烷基、环己基或苯基。硅氮烷也适用。优选使用单-、二-或三甲基氯代甲硅烷、三甲基甲氧基甲硅烷或六甲基二硅氮烷。反应一般在20-100℃,优选30-70℃进行,如果需要,在溶剂如甲苯、丙酮、正己烷、正庚烷、二正丁基醚、异丙醇或甲基异丁基酮中进行。适当时还可以在优选达25巴的压力下进行甲硅烷基化。适当时,干燥前还可以洗涤甲硅烷基化凝胶。
在e)步,甲硅烷基化凝胶在-30℃到溶剂沸点,优点在-30℃到200℃,特别优选在0-150℃的温度下干燥。用于干燥的压力优选为0.001到20巴,特别优选0.01-5巴。一般持续干燥直到溶剂残余含量小于0.1%(重量)。
为了得到特别的热性能,此干凝胶最好另外还含有IR遮光剂(如炭黑、二氧化钛、氧化铁和二氧化锆)。在此情形下,优选在b)步前加入这些IR遮光剂。
以下实施例说明本发明的方法。
实施例
让1升钠水玻璃溶液(含6%(重量)的SiO2,及Na2O∶SiO2之比为2∶3)通过一0.5升酸性离子交换树脂(带磺酸基的苯乙烯/二乙烯基苯共聚物,以Duolite 20的名称在市场上有售)填充的柱子(直径50mm,长度300mm)。流出溶液的PH为1.5。用1摩尔NH4OH溶液调节此溶液PH至5.6。形成的凝胶在50℃老化24小时,然后,在带水分离器的萃取器中于约100℃下用3升甲苯萃取水。当分离出计算量的水(约920ml)后,停止萃取。然后,此含甲苯凝胶在50℃用三甲基氯代甲硅烷(TMCS)甲硅烷基化12小时(0.05gTMCS每克含甲苯凝胶)。在大气压下N2气吹洗下在干燥器中干燥此凝胶(40℃6小时,再50℃2小时,再150℃12小时)。
这样得到的透明干凝胶的密度为0.12g/cm3。BET比表面积为920m2/g。λ值为0.016W/mK。
用热金属线法测定导热率(见,如O.Nielsson,G,Rschenpohler,J.GroB,J.Fricke,High-Temperatures High-Pressures,Vol.21.267-274(1989))。

Claims (8)

1.一种干凝胶的制备方法,其特征在于其包括:
a)用酸性离子交换树脂或无机酸调节水玻璃水溶液至PH≤3.0,
b)加入碱,使由此产生的硅酸缩聚为SiO2凝胶,如果a)步中使用了无机酸,需要时用水洗涤凝胶,直至无电解质为止,
c)用与水形成冷却时分离成两相的共沸物的有机溶剂进行萃取蒸馏,从b)步所得凝胶中除去水,直至凝胶的含水量≤5%(重量),
d)c)步所得凝胶与甲硅烷基化试剂反应,
e)在低于c)步所用有机溶剂的临界压力和/或临界温度的压力和温度下干燥d)步所得甲硅烷基化凝胶。
2.权利要求1的方法,其中a)步中使用酸性离子交换树脂。
3.权利要求1的方法,其中使用NH3OH、NaOH、KOH、Al(OH)3和/或胶态硅酸作为b)步中的碱。
4.权利要求1的方法,其中让b)步所得SiO2凝胶在c)步除水以前于0-150℃及PH4-11老化10秒钟到48小时。
5.权利要求1的方法,其中使用甲苯、二正丁基醚或甲基异丁基酮作为c)步中的有机溶剂。
6.权利要求1的方法,其中使用单-、二-或三甲基氯代甲硅烷、三甲基甲氧基甲硅烷或六甲基二硅氮烷作为d)步中的甲硅烷基化试剂。
7.权利要求1的方法,其中在e)步中于-30℃到200℃干燥甲硅烷基化的凝胶。
8.权利要求1的方法,其中在e)步中于0.001-20巴干燥甲硅烷基化的凝胶。
CN95108111A 1994-06-30 1995-06-28 干凝胶,其制备方法和用途 Expired - Lifetime CN1048696C (zh)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE4422912A DE4422912A1 (de) 1994-06-30 1994-06-30 Xerogele, Verfahren zu ihrer Herstellung, sowie ihre Verwendung
DEP4422912.7 1994-06-30

Publications (2)

Publication Number Publication Date
CN1124229A CN1124229A (zh) 1996-06-12
CN1048696C true CN1048696C (zh) 2000-01-26

Family

ID=6521904

Family Applications (1)

Application Number Title Priority Date Filing Date
CN95108111A Expired - Lifetime CN1048696C (zh) 1994-06-30 1995-06-28 干凝胶,其制备方法和用途

Country Status (8)

Country Link
US (1) US5647962A (zh)
EP (1) EP0690023B1 (zh)
JP (1) JP3808115B2 (zh)
CN (1) CN1048696C (zh)
CA (1) CA2152977A1 (zh)
DE (2) DE4422912A1 (zh)
ES (1) ES2134377T3 (zh)
NO (1) NO952618L (zh)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105031960A (zh) * 2015-08-19 2015-11-11 江西安德力高新科技有限公司 一种醇超临界法生产气凝胶的余热利用装置及工艺

Families Citing this family (47)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5795556A (en) * 1993-12-14 1998-08-18 Hoechst Ag Xerogels and process for their preparation
DE4439217A1 (de) * 1994-11-03 1996-05-09 Hoechst Ag Verfahren zur Herstellung von Aerogelen
DE19502453C1 (de) * 1995-01-27 1996-09-05 Hoechst Ag Verfahren zur Herstellung von modifizierten Si0¶2¶- Aerogelen und deren Verwendung
DE19506141A1 (de) * 1995-02-22 1996-08-29 Hoechst Ag Verwendung von Aerogelen in der Pharmazie, in der Kosmetik und im Pflanzenschutz
DE19533851A1 (de) * 1995-09-13 1997-03-20 Hoechst Ag Organofunktionalisierte Aerogele
DE19541279A1 (de) * 1995-11-06 1997-05-07 Hoechst Ag Verfahren zur Herstellung von organisch modifizierten Aerogelen unter Verwendung von Alkoholen
DE19541992A1 (de) * 1995-11-10 1997-05-15 Hoechst Ag Verfahren zur Herstellung von organisch modifizierten Aerogelen unter Verwendung von Alkoholen, bei dem gebildeten Salze ausgefällt werden
DK0906243T4 (da) * 1996-05-29 2009-06-08 Delsitech Oy Oplöselige oxider til biologiske anvendelser
DE19631267C1 (de) * 1996-08-02 1998-04-30 Hoechst Ag Verfahren zur Herstellung von organisch modifizierten Aerogelen
DE19648798C2 (de) * 1996-11-26 1998-11-19 Hoechst Ag Verfahren zur Herstellung von organisch modifizierten Aerogelen durch Oberflächenmodifikation des wäßrigen Gels (ohne vorherigen Lösungsmitteltausch) und anschließender Trocknung
US5922299A (en) 1996-11-26 1999-07-13 Battelle Memorial Institute Mesoporous-silica films, fibers, and powders by evaporation
US6197270B1 (en) * 1996-12-20 2001-03-06 Matsushita Electric Works, Ltd. Process for producing aerogel
US5807501A (en) * 1997-02-20 1998-09-15 Dow Corning Corporation Neutral-aged hydrophobic organosilicate-modified silica gels
US5789495A (en) * 1997-02-24 1998-08-04 Dow Corning Corporation Method for making hydrophobic organosilicate-modified silica gels under neutral conditions
US5942590A (en) * 1997-02-24 1999-08-24 Dow Corning Corporation Process for making hydrophobic silica with reduced surface area under neutral conditions
US5708069A (en) * 1997-02-24 1998-01-13 Dow Corning Corporation Method for making hydrophobic silica gels under neutral conditions
AU6178498A (en) * 1997-02-24 1998-09-09 Dow Corning Corporation Neutral-aged hydrophobic silica gels with reduced surface area
US6172120B1 (en) * 1997-04-09 2001-01-09 Cabot Corporation Process for producing low density gel compositions
US6071486A (en) * 1997-04-09 2000-06-06 Cabot Corporation Process for producing metal oxide and organo-metal oxide compositions
US6315971B1 (en) * 1997-04-09 2001-11-13 Cabot Corporation Process for producing low density gel compositions
US6235677B1 (en) * 1998-08-20 2001-05-22 Conoco Inc. Fischer-Tropsch processes using xerogel and aerogel catalysts by destabilizing aqueous colloids
US6329017B1 (en) 1998-12-23 2001-12-11 Battelle Memorial Institute Mesoporous silica film from a solution containing a surfactant and methods of making same
US6383466B1 (en) 1998-12-28 2002-05-07 Battelle Memorial Institute Method of dehydroxylating a hydroxylated material and method of making a mesoporous film
US6258864B1 (en) 1999-01-20 2001-07-10 Cabot Corporation Polymer foam containing chemically modified carbonaceous filler
US6586501B1 (en) 1999-01-20 2003-07-01 Cabot Corporation Aggregates having attached polymer groups and polymer foams
US6239243B1 (en) 1999-06-10 2001-05-29 Dow Corning Corporation Method for preparing hydrophilic silica gels with high pore volume
US20040089238A1 (en) * 1999-10-04 2004-05-13 Jerome Birnbaum Vacuum/gas phase reactor for dehydroxylation and alkylation of porous silica
US6656241B1 (en) 2001-06-14 2003-12-02 Ppg Industries Ohio, Inc. Silica-based slurry
WO2003064025A1 (en) * 2002-01-29 2003-08-07 Cabot Corporation Heat resistant aerogel insulation composite and method for its preparation; aerogel binder composition and method for its preparation
EP1511959A2 (en) * 2002-05-15 2005-03-09 Cabot Corporation Heat resistant insulation composite, and method for preparing the same
US20040209066A1 (en) * 2003-04-17 2004-10-21 Swisher Robert G. Polishing pad with window for planarization
US20060089093A1 (en) * 2004-10-27 2006-04-27 Swisher Robert G Polyurethane urea polishing pad
US20060089095A1 (en) * 2004-10-27 2006-04-27 Swisher Robert G Polyurethane urea polishing pad
JP5047488B2 (ja) * 2004-11-05 2012-10-10 ペンタックスリコーイメージング株式会社 シリカエアロゲル膜の製造方法
US7750056B1 (en) 2006-10-03 2010-07-06 Sami Daoud Low-density, high r-value translucent nanocrystallites
KR100824291B1 (ko) * 2007-02-13 2008-04-22 주식회사 넵 표면개질된 나노크기입자의 실리카 제조 방법
WO2009027327A1 (de) * 2007-08-24 2009-03-05 Basf Se Herstellung von metalloxid-nanopartikeln aus alkali-metallaten in organischen lösungsmitteln
KR20090032707A (ko) * 2007-09-28 2009-04-01 엠파워(주) 초소수성 실리카계 분말의 제조방법
DE102009053785A1 (de) 2009-11-19 2011-05-26 BSH Bosch und Siemens Hausgeräte GmbH Verfahren zur Herstellung eines porösen SiO2-Xerogels mit charakteristischer Porengröße durch ein Top-Down-Verfahren über eine Vorstufe mit organischen Festkörperskelettstützen
DE102009053781A1 (de) 2009-11-19 2011-05-26 BSH Bosch und Siemens Hausgeräte GmbH Verfahren zur Herstellung eines porösen SiO2-Xerogels mit charakteristischer Porengröße durch ein Bottom-Up-Verfahren über eine Vorstufe mit Poren, die mit einer organischen Komponente gefüllt sind
DE102009053784A1 (de) 2009-11-19 2011-05-26 BSH Bosch und Siemens Hausgeräte GmbH Verfahren zur Herstellung eines porösen SiO2-Xerogels mit charakteristischer Porengröße durch ein Bottom-Up-Verfahren über eine Vorstufe mit organischen Festkörperskelettstützen
DE102009053780A1 (de) 2009-11-19 2011-05-26 BSH Bosch und Siemens Hausgeräte GmbH Verfahren zur Herstellung eines porösen SiO2-Xerogels mit charakteristischer Porengröße durch ein Top-Down-Verfahren über eine Vorstufe mit Poren, die mit einer organ. oder mit einer Kohlenstoffkomponente gefüllt sind
DE102009053782A1 (de) 2009-11-19 2011-06-01 BSH Bosch und Siemens Hausgeräte GmbH Poröses SiO2-Xerogel mit charakteristischer Porengröße, dessen trocknungsstabile Vorstufen und dessen Anwendung
JP6330145B2 (ja) * 2014-06-17 2018-05-30 パナソニックIpマネジメント株式会社 キセロゲルの製造方法
CN108976803B (zh) * 2018-07-12 2021-07-09 杨帮燕 一种有机防火堵料
EP3896035A1 (en) 2020-04-15 2021-10-20 EMPA Eidgenössische Materialprüfungs- und Forschungsanstalt Silica aerogels and silica aerogel blankets
WO2021204815A1 (en) 2020-04-06 2021-10-14 Empa Eidgenössische Materialprüfungs- Und Forschungsanstalt Silica aerogels

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4938899A (zh) * 1972-08-19 1974-04-11

Family Cites Families (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB682574A (en) * 1950-05-04 1952-11-12 Dow Corning Ltd Improvements in or relating to silica compositions
US3801705A (en) * 1968-10-11 1974-04-02 Nat Petro Chem Preparation of silica gels
US3846537A (en) * 1972-08-21 1974-11-05 Monsanto Co Process of preparing silica xerogels
DE2455535A1 (de) * 1974-11-23 1976-05-26 Basf Ag Verfahren zum herstellen von olefinpolymerisaten
US4190457A (en) * 1978-06-09 1980-02-26 Phillips Petroleum Co. Preparation of inorganic xerogels
CS208879B1 (en) * 1979-07-09 1981-10-30 Ivan Novak Preparation method of silicic acid xerogel with high volumen of pores
US4649037A (en) * 1985-03-29 1987-03-10 Allied Corporation Spray-dried inorganic oxides from non-aqueous gels or solutions
JPS62207712A (ja) * 1986-03-05 1987-09-12 Fuji Debuison Kagaku Kk ビ−ルの安定化処理用含水シリカゲル
DE3914850A1 (de) * 1989-05-05 1990-11-08 Basf Ag Thermisches isoliermaterial auf der basis von pigmenthaltigen kieselsaeureaerogelen
WO1992003378A1 (en) 1990-08-23 1992-03-05 United States Department Of Energy A METHOD FOR PRODUCING METAL OXIDE AEROGELS HAVING DENSITIES LESS THAN 0.02 g/cm?3¿

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4938899A (zh) * 1972-08-19 1974-04-11

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105031960A (zh) * 2015-08-19 2015-11-11 江西安德力高新科技有限公司 一种醇超临界法生产气凝胶的余热利用装置及工艺

Also Published As

Publication number Publication date
EP0690023A3 (de) 1996-04-10
DE4422912A1 (de) 1996-01-11
EP0690023A2 (de) 1996-01-03
CA2152977A1 (en) 1995-12-31
ES2134377T3 (es) 1999-10-01
NO952618D0 (no) 1995-06-29
NO952618L (no) 1996-01-02
EP0690023B1 (de) 1999-05-12
JPH0859224A (ja) 1996-03-05
US5647962A (en) 1997-07-15
CN1124229A (zh) 1996-06-12
JP3808115B2 (ja) 2006-08-09
DE59505881D1 (de) 1999-06-17

Similar Documents

Publication Publication Date Title
CN1048696C (zh) 干凝胶,其制备方法和用途
KR100501758B1 (ko) 형성된염이침전되는유기변성에어로겔의제조방법
KR19980701661A (ko) 개질된 에어로겔의 제조방법 및 이의 용도
JP3854645B2 (ja) キセロゲル、その製法および用途
US5795556A (en) Xerogels and process for their preparation
JPH11514628A (ja) アルコールを使用して有機変性したエーロゲルの製造法
KR101187568B1 (ko) 실리카 에어로겔 과립의 제조방법
US6129949A (en) Process for preparing organically modified aerogels using alcohols, wherein the resultant salts are precipitated
US6156386A (en) Method for the preparation of organically modified aerogels
US5759506A (en) Process for preparing aerogels
KR20000057273A (ko) 유기적으로 변형되어 영구히 소수성인 에어로겔의 제조방법
WO2009038393A2 (en) Method for preparing surface-modified transparent bead type aerogel and aerogel prepared therefrom
JP2001019422A (ja) 高気孔容積を有する親水性シリカゲルの製造法
MXPA97005686A (en) Procedure for the preparation of modified aerogels, and its
MXPA99004858A (es) Proceso para la elaboracion de aerogeles organicos modificados permanentemente hidrofobicos

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C53 Correction of patent of invention or patent application
COR Change of bibliographic data

Free format text: CORRECT: PATENTEE; FROM: HOECHST AKTIENGESELLSCHAFT TO: CABOT CORPORATION

Free format text: CORRECT: PATENTEE; FROM: HOECHST AKTIENGESELLSCHAFT (DE) TO: HOECHST AKTIENGESELLSCHAFT

CP03 Change of name, title or address

Address after: Massachusetts, USA

Patentee after: CABOT Corp.

Address before: Frankfurt, Germany

Patentee before: HOECHST RESEARCH & TECHNOLOGY DEUTSCHLAND GmbH & Co.KG

Patentee after: HOECHST RESEARCH & TECHNOLOGY DEUTSCHLAND GmbH & Co.KG

Patentee before: HOECHST AG

C14 Grant of patent or utility model
GR01 Patent grant
CX01 Expiry of patent term

Expiration termination date: 20150628

Granted publication date: 20000126

EXPY Termination of patent right or utility model