发明名称 |
Initiated chemical vapor deposition of vinyl polymers for the encapsulation of particles |
摘要 |
Described herein are all-dry encapsulation methods that enable well-defined polymers to be applied around particles. One aspect of the invention relates to a method of coating a particle, comprising the steps of: placing said particle in a vessel at a pressure; rotating said vessel at a rotating speed for a period of time; mixing together a first gaseous monomer at a first flow rate, and a gaseous initiator at a second flow rate, thereby forming a mixture; introducing said mixture into said vessel via a vapor feedline; heating said mixture, thereby forming a reactive mixture; contacting said particle with said reactive mixture; thereby forming a polymer coating on said particle. The methods may be modified forms of initiated chemical vapor deposition using a thermally-initiated radical polymerization to create conformal coatings around individual particles while avoiding agglomeration. Particle surfaces may be coated with a range of functional groups. |
申请公布号 |
US9492805(B2) |
申请公布日期 |
2016.11.15 |
申请号 |
US200611589683 |
申请日期 |
2006.10.30 |
申请人 |
Massachusetts Institute of Technology |
发明人 |
Gleason Karen K.;Lau Kenneth K. S. |
分类号 |
B01J13/14;B01J13/04;A61K9/20;A61K9/50;C23C16/44;C23C16/452 |
主分类号 |
B01J13/14 |
代理机构 |
Foley Hoag LLP |
代理人 |
Foley Hoag LLP |
主权项 |
1. A method, comprising the steps of:
placing a plurality of individual particles in a vessel at a pressure; wherein said vessel comprises a vapor feedline for delivering vapors into said vessel through exit holes, and a filament in proximity to said exit holes; the individual particles consist of soda glass, silica, carbon, or a drug; and the diameters of said individual particles are about 5 μm to about 35 μm; contacting said vessel with a water bath at a first temperature, wherein said first temperature is between about 0° C. and about 100° C.; rotating said vessel at a rotating speed for a period of time; mixing together a first gaseous monomer at a first flow rate, and a gaseous initiator at a second flow rate, thereby forming a mixture; introducing said mixture into said vessel via said vapor feedline which comprises said filament at a second temperature, wherein said second temperature is between about 150° C. and 350° C.; heating said mixture with said filament, thereby forming a reactive mixture; contacting said plurality of individual particles with said reactive mixture; thereby forming a plurality of individual coated particles, wherein each individual coated particle consists of a substantially uniform polymer coating encapsulating one individual particle; the thickness of said substantially uniform polymer coating is about 3 μm to about 12 μm; each individual particle is non-agglomerated; and the plurality of individual coated particles is non-agglomerated. |
地址 |
Cambridge MA US |