Classifications

• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
  • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
  • F17C11/00—Use of gas-solvents or gas-sorbents in vessels
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
  • B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
  • B01J13/0091—Preparation of aerogels, e.g. xerogels
• • C—CHEMISTRY; METALLURGY
  • C01—INORGANIC CHEMISTRY
  • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
  • C01B33/00—Silicon; Compounds thereof
  • C01B33/113—Silicon oxides; Hydrates thereof
  • C01B33/12—Silica; Hydrates thereof, e.g. lepidoic silicic acid
  • C01B33/14—Colloidal silica, e.g. dispersions, gels, sols
  • C01B33/157—After-treatment of gels
  • C01B33/158—Purification; Drying; Dehydrating
  • C01B33/1585—Dehydration into aerogels
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
  • Y02C20/00—Capture or disposal of greenhouse gases
  • Y02C20/40—Capture or disposal of greenhouse gases of CO2

Definitions

• Aerogels as a carrier material for propellant systems
• the invention relates to a system for the reversible pressure-dependent storage of gas, consisting of a 3-phase system containing carrier material in solid form (I), solvent in liquid form (II) and gas in thermodynamic equilibrium between the dissolved and gaseous state (III ) and the use of such systems.
• the polymers mentioned in EP 0 385 773 mentioned also have a relatively low solvent absorption capacity, which in turn depends on the gas absorption capacity.
• inorganic polymers and pseudopolymers such as silica gels, zeolites or other silicates are also listed as polymeric materials in the application mentioned.
• inorganic polymers and pseudopolymers such as silica gels, zeolites or other silicates are also listed as polymeric materials in the application mentioned.
• the suitability of these blanket materials as support material for the systems mentioned is not supported in the further description and is not supported by examples. Aerogels as a suitable carrier material are not mentioned.
• Aerogels and their production are also known, for example from Kistler, J. Phys. Chem., 36, (1932), pages 52 to 64.
• SiO 2 aerogels can also be prepared via the hydrolysis of commercially available orthosilica esters.
• aerogels can absorb gases in the sense of a 2-phase system. For example, Parkyns reports in a scientific paper in J. Catal. 27, (1), page 34 ff. On the inclusion of CO 2 in Al 2 O 3 airgel and on IR spectra of the enclosed molecules.
• adsorption elements gas filters which adsorb gases as largely as possible irreversibly under conditions of use and, in this specific case, consist of metal silicate airgel and / or activated carbon incorporated in a matrix.
• the suitability of aerogels as a carrier material in 3-phase systems has not been previously described.
• the object of the invention is to provide a carrier material for a 3-phase system for the reversible pressure-dependent storage of gas, which offers a significantly higher absorption capacity for the solvent than previously known carrier materials for such systems.
• a significant reduction in weight of the carrier material is to be achieved with the same amount of solvent and gas storage capacity.
• the support material should be as universal as possible with regard to the solvents which can be used and should be largely inert to the latter.
• aerogels and their production are known to the person skilled in the art, for example from the Kistler article mentioned.
• water glass is used as the starting product.
• Acidifying water glass with HCl or H 2 SO 4 produces a silica hydrogel, which is then freed from alkali metal ions by washing with water.
• Water contained in the hydrogel is then completely exchanged for 95% alcohol such as ethanol or methanol.
• the resulting SiO 2 alkogel is then supercritically dried in an autoclave.
• SiO 2 alkogels Since the drying of SiO 2 alkogels requires high temperatures and high pressures, a dry process of CO 2 disclosed in EP 0 171 722 was developed, the organic solvent being replaced by CO 2 before the supercritical drying. The supercritical drying from CO 2 takes place at much lower temperatures.
• Another process for the production of SiO 2 aerogels is based directly on SiO 2 alkogels according to DE 18 11 353 and US Pat.
• tetramethoxysilane in methanol or tetraoxysilane in ethanol are mixed with a precisely metered amount of water.
• silicic acid forms with the elimination of alcohol, which in turn forms an SiO 2 gel with the elimination of H 2 O (sol / gel process).
• the resulting alkogel is supercritically dried in an autoclave.
• the carrier material consists essentially of an SiO 2 airgel, which is obtainable by extraction of an intermediate-formed polysilicic acid from acid-treated water glass with an organic solvent and then the solvent-SiO 2 -extact formed with the addition of polysilicic acid esters and / or Bases is subjected to supercritical conditions and the organic solvent is distilled off under relaxation. It may also be preferred that the carrier material consists essentially of an SiO 2 airgel, which can be prepared by gelling one or more polysilicic acid esters under acidic, neutral or alkaline conditions and then subjecting the gel formed to supercritical conditions and then distilling off the alcohol components with relaxation become.
• aerogels of the most varied inorganic compounds or mixtures thereof can be used.
• examples include Al 2 O 3 aerogels or the metal silicate aerogels listed in DE 39 37863 or also TiO 2 -based aerogels.
• the carrier material used according to the invention is largely inert, there are practically no restrictions with regard to the solvents.
• Polar liquids are preferably used. For example, tetraethyl glycol dimethyl ether, ethanol, isobutyl acetate, diethyl ether, methyl acetate and / or acetone are considered suitable.
• Methyl acetate and / or acetone are preferred since, among other things, they have a very good absorption capacity for gases, in particular for carbon dioxide. Mixtures of two or more solvents can also be used, for example mixtures of acetone and water.
• the systems according to the invention for the reversible, pressure-dependent storage of gas are used above all in compressed gas packs, in particular in two-chamber pressurized gas packs. Suitable pressurized gas packs are described in EP 0 385 773 already mentioned. At this point, reference should once again be made expressly to this European application. The disclosure content of EP 0 385 773 and the Unless they relate to the polymeric organic carrier material, the particular embodiments listed there can be transferred to the present invention.
• the present systems according to the invention are used in particular in compressed gas packs, preferably two-chamber compressed gas packs.
• the blowing agent systems are particularly suitable for use in pressurized gas packs for dispensing a liquid to pasty material, in particular joint sealants, foams and adhesives.
• the advantages of the systems according to the invention for reversible, pressure-dependent storage of gas, in particular when using them, are, on the one hand, that, with the same gas storage capacity and otherwise equivalent application properties, the amount of the carrier material, e.g. compared to the hydrogel preferred in EP 0 385 773 can be reduced to a fifth.
• the inorganic aerogels are non-combustible compared to the organic polymers.
• any organic liquid can be used when using aerogels as the carrier material, while when using organic polymers as the carrier material only those organic liquids can be used which do not dissolve the polymer.
• the aerogels can therefore be used more universally.
• Airgel (according to 10.0 11.0
• Airgel (according to 10.0 11.0
• the information in the table is to be understood to mean that, for example, one unit by weight of hydrogel (according to EP 0 385 773) has a solvent absorption capacity of 1.1 unit by weight of acetone.

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• 1991
  • 1991-02-04 DE DE4103280A patent/DE4103280A1/de not_active Withdrawn
• 1992
  • 1992-01-24 WO PCT/EP1992/000151 patent/WO1992014091A1/de not_active Application Discontinuation
  • 1992-01-24 JP JP4503496A patent/JPH06504976A/ja active Pending
  • 1992-01-24 AU AU11702/92A patent/AU644515B2/en not_active Ceased
  • 1992-01-24 EP EP92904386A patent/EP0571438A1/de not_active Withdrawn

Non-Patent Citations (1)

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