Patent classifications
A61L29/06
Biomedical devices
A biomedical device is disclosed which is a polymerization product of a mixture comprising (a) one or more difunctional isocyanates; (b) one or more polyalcohols; (c) one or more hydroxy-terminated polysiloxane prepolymers; and (d) one or more polyoxazoline polyols having a weight average molecular weight of equal to or greater than about 1000 Daltons.
MEDICAL SYSTEM INCLUDING STEERABLE CATHETER AND METHOD OF MANUFACTURING
A steerable catheter may include an elongate shaft member and a braided reinforcement structure embedded into a wall of the elongate shaft member. The braided reinforcement structure may include a first braided portion including a first pick count, a second braided portion including a second pick count, and a third braided portion including a third pick count. The third pick count may be greater than each of the first pick count and the second pick count.
MEDICAL SYSTEM INCLUDING STEERABLE CATHETER AND METHOD OF MANUFACTURING
A steerable catheter may include an elongate shaft member and a braided reinforcement structure embedded into a wall of the elongate shaft member. The braided reinforcement structure may include a first braided portion including a first pick count, a second braided portion including a second pick count, and a third braided portion including a third pick count. The third pick count may be greater than each of the first pick count and the second pick count.
COMPOUNDED ACTIVE PHARMACEUTICAL AGENTS IN THERMOPLASTIC POLYMER COMPOSITIONS AND METHODS OF MANUFACTURE
In a method of integrating an active pharmaceutical ingredient (API) with a thermoplastic polymer, the thermoplastic polymer and API are into a first feed port of a multi-screw extruder or the thermoplastic polymer is fed into the first feed port of a multi-screw extruder, the thermoplastic polymer is conveyed along the heated multi-screw extruder while heating the thermoplastic polymer to a melt temperature of 160° C.-280° C. prior to the thermoplastic polymer being conveyed past a second feed port and the API is fed into the second feeding port in the heated screw extruder to mix with the melted thermoplastic polymer to generate a compounded mixture containing 85-100% of the starting API content. The compounded mixture is extruded from an outlet of the heated screw extruder and cooled via a cooling device such that the compounded mixture contains 85-100% of the starting API content.
COMPOUNDED ACTIVE PHARMACEUTICAL AGENTS IN THERMOPLASTIC POLYMER COMPOSITIONS AND METHODS OF MANUFACTURE
In a method of integrating an active pharmaceutical ingredient (API) with a thermoplastic polymer, the thermoplastic polymer and API are into a first feed port of a multi-screw extruder or the thermoplastic polymer is fed into the first feed port of a multi-screw extruder, the thermoplastic polymer is conveyed along the heated multi-screw extruder while heating the thermoplastic polymer to a melt temperature of 160° C.-280° C. prior to the thermoplastic polymer being conveyed past a second feed port and the API is fed into the second feeding port in the heated screw extruder to mix with the melted thermoplastic polymer to generate a compounded mixture containing 85-100% of the starting API content. The compounded mixture is extruded from an outlet of the heated screw extruder and cooled via a cooling device such that the compounded mixture contains 85-100% of the starting API content.
COMPOUNDED ACTIVE PHARMACEUTICAL AGENTS IN THERMOPLASTIC POLYMER COMPOSITIONS AND METHODS OF MANUFACTURE
In a method of integrating an active pharmaceutical ingredient (API) with a thermoplastic polymer, the thermoplastic polymer and API are into a first feed port of a multi-screw extruder or the thermoplastic polymer is fed into the first feed port of a multi-screw extruder, the thermoplastic polymer is conveyed along the heated multi-screw extruder while heating the thermoplastic polymer to a melt temperature of 160° C.-280° C. prior to the thermoplastic polymer being conveyed past a second feed port and the API is fed into the second feeding port in the heated screw extruder to mix with the melted thermoplastic polymer to generate a compounded mixture containing 85-100% of the starting API content. The compounded mixture is extruded from an outlet of the heated screw extruder and cooled via a cooling device such that the compounded mixture contains 85-100% of the starting API content.
DRUG-COATED BALLOON CATHETERS FOR BODY LUMENS
Various embodiments disclosed relate to drug-coated balloon catheters for treating strictures in body lumens and methods of using the same. A drug-coated balloon catheter for delivering a therapeutic agent to a target site of a body lumen stricture includes an elongated balloon having a main diameter. The balloon catheter includes a coating layer overlying an exterior surface of the balloon. The coating layer includes one or more water-soluble additives and an initial drug load of a therapeutic agent.
DRUG-COATED BALLOON CATHETERS FOR BODY LUMENS
Various embodiments disclosed relate to drug-coated balloon catheters for treating strictures in body lumens and methods of using the same. A drug-coated balloon catheter for delivering a therapeutic agent to a target site of a body lumen stricture includes an elongated balloon having a main diameter. The balloon catheter includes a coating layer overlying an exterior surface of the balloon. The coating layer includes one or more water-soluble additives and an initial drug load of a therapeutic agent.
A MEDICAL TUBING COMPRISING THERMOPLASTIC POLYURETHANE
A medical tubing contains a thermoplastic polyurethane.
A MEDICAL TUBING COMPRISING THERMOPLASTIC POLYURETHANE
A medical tubing contains a thermoplastic polyurethane.