US3958014A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for preparing injection-purpose fluorocarbon emulsion capable of carrying oxygen
Assignee: Tanabe Pharma Corp
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Filing: 1973-03-20
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Granted: 1976-05-18
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Expires: 1993-03-20
Abstract
Abstract An injectable fluorocarbon emulsion capable of carrying oxygen, which can be used as artificial blood and organ perfusate, is prepared by emulsifying a fluorocarbon, having an ability to dissolve at least 30 V/V % of oxygen under a 100% oxygen atmosphere at an atmospheric pressure, in an aqueous salt solution with a surfactant, centrifuging the resulting aqueous emulsion thereby to reduce the fluorocarbon particles in the emulsion in size to particle sizes of the order of about 0.05 to 0.25 mu , and then sterilizing the thus obtained emulsion under rotation. The resulting fluorocarbon emulsion can be used as an emergency blood substitute for transfusion.
Inventors
- 👤 Ryozo Watanabe
- 👤 Tadakazu Suyama
- 👤 Kazumasa Yokoyama
- 👤 Yohei Odaka
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-23 17:21
CPC Classifications
A; A61; A61K; A61K9/00; A61K9/0012; A61K9/0019; A61K9/0026; A61K31/00; A61K31/02; C; C09; C09K; C09K23/00; C09K23/14
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
288 words
A process for preparing an injectable emulsion of fluorocarbon particles adapted to carry oxygen in an aqueous vehicle, said process comprising a. emulsifying an aqueous physiologically acceptable electrolyte solution containing from about 10 up to at most about 30 W/V %, based on the emulsion, of a fluorocarbon selected from the group consisting of perfluorodecalin, perfluoromethyldecalin and their mixture and from about 3 W/V % to about 5 W/V %, based on the emulsion, of yolk lecithin, and continuing the emulsification until said fluorocarbon particles are dispersed in the aqueous phase and distributed in a particle range size of from about 0.05 to about 1.0 microns by injecting the emulsion with a Manton-Gaulin type injection emulsifier under a pressure of 140 kg/cm 2 at the first stage, under a pressure of 500 kg/cm 2 at the second and third stages, under a pressure of 560 kg/cm 2 at the fourth stage and under a pressure of 140 kg/cm 2 at the fifth stage at 50° C or less; b. continuously centrifuging the aqueous emulsion of step (a) with a De Laval type centrifuge at a flow rate of 30 l/hour while setting the mortar and the rotor at 1500 rpm. and 9000 rpm, respectively, or with a Saval type centrifuge at a flow rate of 6 l hour, while setting the centrifuge at 100 × g, thereby reducing the particle size of said fluorocarbon particles into particles of the order of about 0.05 to about 0.25 microns and c. subjecting the aqueous emulsion of step (b) to sterilization at 110° to 120° C for 15 minutes while rotating said emulsion at 15 rpm, thereby preventing substantial agglomeration of said fluorocarbon particles in said emulsion while sterilizing said emulsion.
Claim 2
Dependent Claim
288 words
A process for preparing an injectable emulsion of fluorocarbon particles adapted to carry oxygen in an aqueous vehicle, said process comprising a. emulsifying an aqueous physiologically acceptable electrolyte solution containing from about 10 up to at most about 30 W/V %, based on the emulsion, of a fluorocarbon selected from the group consisting of perfluorodecalin, perfluoromethyldecalin and their mixture and from about 3 W/V % to about 5 W/V %, based on the emulsion, of yolk lecithin, and continuing the emulsification until said fluorocarbon particles are dispersed in the aqueous phase and distributed in a particle range size of from about 0.05 to about 1.0 microns by injecting the emulsion with a Manton-Gaulin type injection emulsifier under a pressure of 140 kg/cm 2 at the first stage, under a pressure of 500 kg/cm 2 at the second and third stages, under a pressure of 560 kg/cm 2 at the fourth stage and under a pressure of 140 kg/cm 2 at the fifth stage at 50° C or less; b. continuously centrifuging the aqueous emulsion of step (a) with a De Laval type centrifuge at a flow rate of 30 l/hour while setting the mortar and the rotor at 1500 rpm. and 9000 rpm, respectively, or with a Saval type centrifuge at a flow rate of 6 l hour, while setting the centrifuge at 100 × g, thereby reducing the particle size of said fluorocarbon particles into particles of the order of about 0.05 to about 0.25 microns and c. subjecting the aqueous emulsion of step (b) to sterilization at 110° to 120° C for 15 minutes while rotating said emulsion at 15 rpm, thereby preventing substantial agglomeration of said fluorocarbon particles in said emulsion while sterilizing said emulsion.
Claim 3
Dependent Claim
27 words
The process of claim 1, wherein the particle size of said fluorocarbon particles following step (c) is of the order of about 0.05 to about 0.375 microns.
Claim 4
Dependent Claim
20 words
The process of claim 1, wherein the amount of said fluorocarbon is from about 25 to about 30 W/V %.
References Cited (Backward Citations)
No citation records indexed.
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-05-18 | 1979-11-17 | 1980-05-18 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-05-18 | 1983-11-17 | 1984-05-18 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-05-18 | 1987-11-17 | 1988-05-18 | $7700.00 | Window Closed / Lapsed |