Coating processes – Particles – flakes – or granules coated or encapsulated – Inorganic base
Reexamination Certificate
1998-08-24
2001-04-03
Beck, Shrive (Department: 1762)
Coating processes
Particles, flakes, or granules coated or encapsulated
Inorganic base
C427S212000, C427S215000, C516S081000, C516S082000, C516S085000
Reexamination Certificate
active
06210751
ABSTRACT:
The present invention relates to a process for the preparation of organically modified SiO
2
aerogels, in which process the salts formed are precipitated.
Aerogels, particularly those having porosities over 60% and densities below 0.6 g/cm
3
have an extremely low thermal conductivity and for this reason are used as thermal insulating materials, as described e.g. in EP-A-0 171 722.
Aerogels in the broader sense of the term, i.e. in the sense of a “gel with air as dispersing agent,” are prepared by drying a suitable gel. Understood by the term “aerogel” in this sense are aerogels considered in the narrower sense, xerogels and cryogels. A dried gel is considered an aerogel in the narrower sense of the term when the liquid of the gel is removed at temperatures above the critical temperature and starting from pressures above the critical pressure. However, if the liquid of the gel is removed under subcritical conditions, e.g. with the formation of a liquid-vapor boundary phase, then the resulting gel is designated as a xerogel. It should be noted that the gels according to the invention are aerogels in the sense of gels with air as dispersing agent.
SO
2
aerogels can be prepared e.g. by acid hydrolysis of tetraethyl orthosilicate in ethanol. During the hydrolysis a gel is formed whose structure is determined, among other things, by the temperature, the pH and the duration of the gelation process. However, during the drying of the wet gels, the gel structure generally collapses because the capillary forces resulting during drying are extremely great. Collapse of the gel can be prevented by carrying out the drying above the critical temperature and critical pressure of the solvent. Since in this range the liquid/gas phase boundary disappears, the capillary forces also vanish and the gel does not change during the drying process, i.e. no shrinking of the gel will occur during the drying, either. Methods of preparation based on this drying technology are disclosed e.g. in EP-A-0 396 076 and WO 92/03378. However, e.g. when ethanol is used, this technique requires a temperature of about 240° C. and pressures over 60 bar. Although the exchange of ethanol against CO
2
before drying does reduce the drying temperature to about 30° C., the pressure required is then over 70 bar.
An alternative to the above drying method is offered by a process of subcritical drying of SiO
2
gels, if, before drying, the latter are reacted with a chlorine-containing silylating agent. In that case the SiO
2
gel can be obtained e.g. by acid hydrolysis of tetraalkoxysilanes, preferably tetraethoxysilane (TEOS) in a suitable organic solvent, preferably ethanol, by means of water. In a further step, after exchange of the solvent against a suitable organic solvent, the resulting gel is reacted with a chlorine-containing silylating agent. Used as silylating agents, because of their reactivity, are preferably methylchlorosilanes (Me
4−n
SiCl
n
, with n=1 to 3). Thereupon the resulting SiO
2
gel whose surface has been modified by methylsilyl groups, can be dried in air from an organic solvent. In this way aerogels having densities of less than 0.4 g/cm
3
and porosities over 60% can be obtained.
WO 94/25149 gives a detailed description of the method of preparation based on this drying technique.
Furthermore, before drying, the above-described gels can be treated in the aqueous alcoholic solution with tetraalkoxysilanes, and then aged, in order to increase the strength of the gel network, as disclosed e.g. in WO 92/20623.
However, the tetraalkoxysilanes used as starting materials in the above-described process are extremely expensive.
A first, not inconsiderable cost reduction can be achieved by using water glass as the starting material for the preparation of the SiO
2
gels. To this end, a silicic acid can be prepared, e.g., from an aqueous water glass solution with the aid of an ion exchanger resin, which acid will polycondense to a SiO
2
gel upon the addition of a base. Then in a further step, after exchange of the aqueous medium against a suitable organic solvent, the resulting gel is reacted with a chlorine-containing silylating agent. Used as silylating agents, because of their reactivity, are again preferably methylchlorosilanes (Me
4−n
SiCl
n
with n=1 to 3). The resulting SiO
2
gel surface-modified with methylsilyl groups can then also be dried in air from an organic solvent. The method of preparation based on this technique is described e.g. in DE-A-43 42 548.
An unsolved problem consists in the aqueous salt solutions which are obtained in the preparation of aerogels from water glass. In order to convert a water glass solution into a silicic acid sol capable of condensation, the cations (mostly sodium and/or potassium ions) must be exchanged in the water glass solution against protons. For this purpose, organic and/or inorganic acids may be used. The salts of the above-mentioned cations (e.g. NaCl or Na
2
SO
4
) which will also necessarily be formed in the dissolved state must be washed out from the gel before, during or after gel aging. At present, these highly dilute aqueous salt solutions constitute a great disposal problem, because they can no longer be discharged into rivers or lakes in relatively large quantities. A final disposal of these solutions which meets current regulations represents an extremely high cost factor. The preparation of a silica sol from water glass and sulfuric acid, and crystallization and separation of the resulting sodium sulfate by cooling the reaction mixture is known from U.S. Pat. No. 2,285,477.
The object of the present invention was to provide a process for the preparation of organically modified SiO
2
aerogels in which no dilute aqueous salt solutions will be formed.
This object is met by a process for the preparation of organically modified aerogels, comprising
a) the preparation of a silicic acid sol having a pH of ≦4.0 from an aqueous water solution, with the aid of at least one organic and/or inorganic acid;
b) polycondensation of the resulting silicic acid sol to a SiO
2
gel by the addition of a base;
c) washing the gel obtained in Step b) with an organic solvent until the water content of the gel is ≦5% by weight;
d) surface-silylating the gel obtained in Step c), and
e) drying the surface-modified gel obtained in Step d), characterized in that the salts formed from the acid and the cations of the water glass are extensively precipitated before Step b) at temperatures of 0 to 30° C. and separated from the silicic acid sol.
Used as water glass solution in Step a) is generally a 6 to 25% by weight (calculated on the SiO
2
content) sodium and/or potassium water glass solution. A 17 to 20% by weight water glass solution is preferred. Furthermore, the water glass solution may also contain up to 90% by weight (calculated on SiO
2
) of zirconium, aluminum and/or titanium compounds capable of condensation.
The acids used are generally 15 to 50% by weight acids, which form difficultly soluble salts with sodium and/or potassium ions. Mixtures of suitable acids can also be used. Sulfuric, phosphoric, hydrofluoric and oxalic acid are preferred. Sulfuric acid is especially preferred.
To achieve an as complete precipitation and good separation of the difficultly soluble salts formed in Step a) as possible, the silicic acid sol should have a temperature between 0 and 30° C., preferably between 0 and 15° C., and by particular preference between 0 and 5° C. This can be achieved by bringing the water glass solution, the acid and/or the silicic acid sol to a temperature between 0 and 30° C., preferably between 0 and 15° C., and by particular preference between 0 and 5° C. If, in so doing, a supersaturated salt solution should form, the salt can be precipitated by suitable seeding with appropriate seeding crystals. The salts formed are separated by means known to persons skilled in the art, e.g. by filtration, sintering, suction filtration, membranes or crystallization vessels. Semi-continuous or continuous processes are preferred.
After the s
Beck Shrive
Cabot Corporation
Frommer & Lawrence & Haug LLP
Strain Paul D.
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