US5942574A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for continuously emulsifying organopolysiloxane gums
Assignee: DuPont Toray Specialty Materials KK
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Filing: 1998-01-12
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Granted: 1999-08-24
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Expires: 2018-01-12
Abstract
Abstract A method of continuous emulsification that can emulsify high-viscosity organopolysiloxane gums and is capable of continuous mass production. A compounding extruder is used whose barrel 1 contains at least 2 mixing element-equipped shafts 3 installed in parallel. On each shaft elevations and depressions are formed along the axial direction and the elevations and depressions on respective shafts intermesh. Organopolysiloxane gum, emulsifying agent, and water are continuously supplied as starting materials to this compounding extruder, and an organopolysiloxane-in-water emulsion is produced by mixing and homogenizing the starting materials by subjecting them through rotation of the mixing element-equipped shafts to a shearing action at a shear rate of at least 10/second (i.e. 10 reciprocal seconds).
Inventors
- 👤 Hidehiko Hosokawa
- 👤 Junichi Maeshima
- 👤 Fumitaka Suto
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 12:40
CPC Classifications
C; C08; C08J; C08J3/00; C08J3/02; C08J3/03; B; B01; B01F; B01F23/00; B01F23/40; B01F23/47; B01F27/00; B01F27/60; B01F27/70; B01F27/701; B01F27/702; B29; B29B; B29B7/00; B29B7/30; B29B7/34; B29B7/38; B29B7/46; B29B7/48; B29B7/482; B29B7/483; B29B7/488; B29B7/489; B29B7/74; B29B7/7476; B29B7/7495; B29C; B29C48/00; B29C48/25; B29C48/36; B29C48/395; B29C48/40; B29C48/50; B29C48/505; B29C48/625; B29C48/68; B29C48/682; B01F23/41; C08J2383/00; C08J2383/04
Claims Analysis
Total Claims: 6
Claim 1
Independent Claim
213 words
A method for continuously emulsifying organopolysiloxane gums comprising continuously feeding an organopolysiloxane gum, an emulsifying agent, and water, as starting materials, into a compounding extruder having a supply port and a discharge port, the compounding extruder having a barrel with an eight-shaped transverse cross-section, wherein the barrel contains at least two mixing element-equipped shafts arranged in parallel, each shaft having elevations and depressions formed along the axial direction in alternating sequence, the elevations and depressions on one shaft intermeshing with the elevations and depressions on the other shaft; the elevations and depressions being formed by a plurality of lens-shaped paddles on the shafts; the lens-shaped paddles being attached on the shafts as groups of 2-4 lens-shaped paddles, each group of paddles having the same angle of attachment, but with the angle of attachment of alternating sequences of paddle groups on each shaft being staggered in different increments of 15°, 30° or 45°, with respect to one another; and the mixing element equipped shafts including a screw, producing an organopolysiloxane-in-water emulsion by mixing and homogenizing the starting materials by subjecting the starting materials, through rotation of the mixing element-equipped shafts, to a shearing action at a shear rate of at least 10/second; and discharging the emulsion from the discharge port of the compounding extruder.
Claim 2
Independent Claim
213 words
A method for continuously emulsifying organopolysiloxane gums comprising continuously feeding an organopolysiloxane gum, an emulsifying agent, and water, as starting materials, into a compounding extruder having a supply port and a discharge port, the compounding extruder having a barrel with an eight-shaped transverse cross-section, wherein the barrel contains at least two mixing element-equipped shafts arranged in parallel, each shaft having elevations and depressions formed along the axial direction in alternating sequence, the elevations and depressions on one shaft intermeshing with the elevations and depressions on the other shaft; the elevations and depressions being formed by a plurality of lens-shaped paddles on the shafts; the lens-shaped paddles being attached on the shafts as groups of 2-4 lens-shaped paddles, each group of paddles having the same angle of attachment, but with the angle of attachment of alternating sequences of paddle groups on each shaft being staggered in different increments of 15°, 30° or 45°, with respect to one another; and the mixing element equipped shafts including a screw, producing an organopolysiloxane-in-water emulsion by mixing and homogenizing the starting materials by subjecting the starting materials, through rotation of the mixing element-equipped shafts, to a shearing action at a shear rate of at least 10/second; and discharging the emulsion from the discharge port of the compounding extruder.
Claim 3
Dependent Claim
41 words
A method according to claim 1 wherein the L/D ratio of the mixing element-equipped shafts is at least five, in which L is the length within the barrel of the mixing element-equipped shafts and D is the diameter of the shafts.
Claim 4
Dependent Claim
30 words
A method according to claim 2 wherein the organopolysiloxane gum has a plasticity at 25° C. of at least 0.75 mm, plasticity being determined according to Japanese Industrial Standard C2123.
Claim 5
Dependent Claim
19 words
A method according to claim 2 wherein the organopolysiloxane gum has a viscosity of 500,000-10,000,000 centipoise at 25° C.
Claim 6
Dependent Claim
30 words
A method according to claim 1 wherein the starting materials include 0.1-100 weight parts of emulsifying agent, 1-400 weight parts of water, and 100 weight parts of the organopolysiloxane gum.
References Cited (Backward Citations)
US5806975A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 2002-08-23 | 2003-02-22 | 2003-08-24 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 2006-08-23 | 2007-02-22 | 2007-08-24 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2010-08-23 | 2011-02-22 | 2011-08-24 | $7700.00 | Window Closed / Lapsed |