IP Library Granted Patent US 9,221,690
Granted Patent B2
US 9,221,690 · App. 13/702,676 · Granted Dec 29, 2015

Process for producing a silica sol material

Inventors: Ekkehard Barth (Köln, DE); Rolf Bachmann (Bergisch Gladbach, DE); Arne Braun (Leverkusen, DE); Maren Heinemann (Bergisch Gladbach, DE); Sebastian Schmidt (Lubbock, TX)
Assignee: JIANGSU SYNECOUN MEDICAL TECHNOLOGY CO., LTD
C01B33/141C01B33/14C01B33/145C01B33/148C04B35/624C04B35/6224C04B35/6263C04B35/62635C04B35/62685C08L83/02C04B2235/3418C04B2235/441
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Quick Facts
Patent No.
US 9,221,690
App. No.
13/702,676
Granted
Dec 29, 2015
Kind
B2
Abstract

The present invention relates to an improved process for producing a biodegradable and/or absorbable silica sol material which is advantageous especially with regard to the reproducibility of the material, the rapidity of the synthesis and the possibility of being able to produce the silica sol material on an industrial scale. A further subject matter of the invention relates to a biodegradable and/or absorbable silica sol material which can be produced by the synthesis process according to the invention.

Claims (14)

1. A method for producing a silica sol material by

(a) controlled bringing together of an aqueous acid solution and a hydrolysable silicon compound,

(b) subsequent evaporation to give a single-phase solution with a viscosity in a range from 0.5 to 30 Pa·s at a shear rate of 10 s −1 at 4° C., and

(c) ripening of the single-phase solution obtained in (b) to give a silica sol material with a viscosity from 30 to 100 Pa·s at a shear rate of 10 s −1 at 4° C. and a loss factor of from 2 to 5;

wherein a) is carried out under isothermal conditions,

wherein the ripening in c) is carried out with stirring of the single-phase solution, and

wherein a) to c) is carried out in the same reaction vessel.

2. A method according to claim 1 , wherein the controlled metered addition in a) takes place over a period of at least 15 minutes.

3. A method according to claim 1 , wherein b) is carried out in a closed apparatus and wherein a temperature in b) is kept constant by regulating pressure of said closed apparatus.

4. A method according to claim 1 , wherein the ripening in c) is carried out at a temperature of from 25° C. to 78° C. under a standard pressure of 1 atm or at a temperature >78° C. at superatmospheric pressure.

5. A method according to claim 1 , wherein the ripening in c) is carried out at a temperature from 25° C. to 35° C.

6. A method according to claim 1 , wherein the hydrolysable silicon compound comprises an Si compound of formula SiX 4 ,

in which the radicals X are identical or different and are hydroxyl, hydrogen, halogen, amino, alkoxy, acyloxy, alkylcarbonyl and/or alkoxycarbonyl and are derived from alkyl radicals which are optionally substituted straight-chain, branched or cyclic radicals having 1 to 20 carbon atoms, optionally having 1 to 10 carbon atoms, and can be interrupted by oxygen or sulphur atoms or by amino groups.

7. A method according to claim 1 , wherein the hydrolysable silicon compound comprises tetraethoxysilane.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 24, 2015
From: BAYER INNOVATION GMBH
To: SYNECON (SUZHOU) CO., LTD.
Reel/Frame 035894/0199 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 24, 2015
From: SYNECON (SUZHOU) CO., LTD.
To: JIANGSU SYNECOUN MEDICAL TECHNOLOGY CO., LTD.
Reel/Frame 035894/0268 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 9, 2013
From: BARTH, EKKEHARD, DR.; BACHMANN, ROLF, DR.; BRAUN, ARNE; HEINEMANN, MAREN, DR.; SCHMIDT, SEBASTIAN, DR.
To: BAYER INNOVATION GMBH
Reel/Frame 030178/0623 →
Priority Claims (1)
DE 10 2010 023 336 · Jun 10, 2010 · national
Continuity (1)
Related Publication 20130145964A1 · Jun 13, 2013