Method for formation of micro-prilled polymers
US-2015374629-A1 · Dec 31, 2015 · US
US9669565B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9669565-B2 |
| Application number | US-201314397715-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 30, 2013 |
| Priority date | May 2, 2012 |
| Publication date | Jun 6, 2017 |
| Grant date | Jun 6, 2017 |
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A method for producing particles, which contains: bringing a compressive fluid and a pressure plastic material into contact with each other to melt the pressure plastic material; and jetting a melt obtained by melting the pressure plastic material to form particles, wherein the jetting the melt is performed by a two-fluid nozzle or three-fluid nozzle.
Opening claim text (preview).
The invention claimed is: 1. A method for producing particles, comprising: contacting a first compressive fluid with a pressure plastic material, thereby producing a melt; and jetting the melt, thereby forming particles, wherein the jetting is performed with a three-fluid nozzle in which a third-fluid nozzle supplies a second compressive fluid to an outer circumference of a two-fluid nozzle that supplies the first compressive fluid and the melt, and wherein the first compressive fluid comprises carbon dioxide in a super critical state, and the second compressive fluid comprises nitrogen in a super critical state. 2. The method according to claim 1 , wherein the pressure plastic material is a resin comprising a carbonyl structure. 3. The method according to claim 1 , wherein a viscosity of the melt is 20 mPa·s or lower at a temperature and pressure while jetting. 4. The method according to claim 1 , wherein both the contacting and jetting are continuous thereby continuously forming particles. 5. The method according to claim 4 , wherein the contacting is continuous and does not comprise the use of a static mixer. 6. The method according to claim 1 , wherein the first compressive fluid comprises carbon dioxide. 7. The method according to claim 1 , wherein contacting the compressive fluid and the pressure plastic material further comprises heating and plasticizing the pressure plastic material prior to contacting with the fluid. 8. Particles, comprising: substantially no organic solvent, wherein the particles are obtained by contacting a first compressive fluid and a pressure plastic material with each other thereby producing a melt, and jetting the melt to form the particles, wherein the jetting is performed with a three-fluid nozzle in which a third-fluid nozzle supplies a second compressive fluid to an outer circumference of a two-fluid nozzle that supplies the first compressive fluid and the melt, and wherein the first compressive fluid comprises carbon dioxide in a super critical state, and the second compressive fluid comprises nitrogen in a super critical state. 9. The particles according to claim 8 , wherein a ratio of a volume average particle diameter (Dv) to a number average particle diameter (Dn) of the particles, Dv/Dn, is from 1.0 to 1.10. 10. The method according to claim 1 , wherein a ratio of a volume average particle diameter (Dv) to a number average particle diameter (Dn) of the particles, Dv/Dn, is from 1.0 to 1.10.
Use of {PU, i.e.} polyureas or polyurethanes {or derivatives thereof}, as moulding material · CPC title
Dicarboxylic acids, esters of polycarboxylic acids containing two carboxylic acid groups · CPC title
with gas and liquid jets intersecting in the mixing chamber · CPC title
in a gaseous medium {(if combined with suspending the material in a gas, e.g. fluidised beds B01J2/16)} · CPC title
the annular gas outlet being supplied by a gas conduit having an axially concave curved internal surface just upstream said outlet · CPC title
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