Equipment assembly for and method of processing particles
US-9233348-B2 · Jan 12, 2016 · US
US9925512B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9925512-B2 |
| Application number | US-201514852811-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 14, 2015 |
| Priority date | Mar 14, 2013 |
| Publication date | Mar 27, 2018 |
| Grant date | Mar 27, 2018 |
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An equipment assembly for preparing, harvesting and collecting particles is disclosed. The assembly comprises a tandem filter system with one or more high pressure filters, one or more low pressure filters and one or more collection vessel. Particles can be prepared, harvested and collected continuously, semi-continuously or in a batch-type operation. A tandem filter system and its method of use are also disclosed. Particles made with the assembly and according the instant methods are also disclosed. The assembly provides improved particle harvesting and collection over other systems and permits continuous particle formation, in particular by dispersion of a solute-containing process fluid within a supercritical anti-solvent.
Opening claim text (preview).
The invention claimed is: 1. A particle formation and collection equipment assembly comprising: a) a high pressure particle formation system that forms a particle-containing high pressure liquid suspension; b) at least one high pressure harvesting filter system that receives and filters the particle-containing high pressure liquid suspension, wherein the high pressure particle harvesting filter system comprises: a high pressure housing defining a lengthwise process cavity comprising a downwardly-pointing conical portion, at least one inlet port and at least one outlet port; a liquid particle suspension supply line engaged with the inlet port and configured to provide a high pressure liquid particle suspension comprising particles and anti-solvent; a gas supply line engaged with the outlet port and configured to provide a low-pressure inert gas; a temperature controller for controlling the temperature of the housing; and at least one lengthwise porous element extending into the cavity and comprising a porous wall defining a lengthwise inner conduit engaged with the at least one outlet port, wherein, the porous element is engaged directly or indirectly with the outlet port; the filter system is configured to receive high pressure particle suspension in a first forward process direction and to receive a low pressure inert gas in a second reverse process direction, wherein process direction is with respect to flow through the porous element; c) at least one collection vessel system, downstream of the harvesting filter, that receives the particle-containing low pressure gaseous suspension from the harvesting filter and collects particles; and d) at least one low pressure collection filter system, conductively engaged with and downstream of the at least one collection vessel, that separates gas from particles in the particle-containing low pressure gaseous suspension and retains particles in the collection vessel. 2. The equipment assembly of claim 1 further comprising: a) one or more temperature controllers for one or more of the precipitation chamber, collection filter, emptying filter and collection vessel; b) one or more valves; c) one or more actuators; d) one or more back pressure regulators; d) one or more flow controllers; e) a gas pulsing system configured to pulse gas into at least the harvesting filter; f) one or more computers having a memory storage medium containing software or logic adapted to control operation of one or more components of the system; g) one or more pressure sensors; h) one or more valves that direct flow of a liquid particle suspension to the harvesting filter and direct flow of a gaseous particle suspension from the harvesting filter to the collection filter; i) one or more pumps; j) one or more temperature sensors; k) one or more SCF supply systems; l) one or more process fluid supply systems; m) one or more pumps for pumping process fluid, supercritical carbon dioxide (scCO 2 ) or a combination of process fluid and scCO 2 ; n) one or more solvent separation vessels; o) one or more solvent collection vessels; and/or p) one or more in-line sensors. 3. The equipment assembly of claim 2 comprising at least one temperature controller, at least one temperature sensor, at least one pressure sensor, at least one back pressure regulator, at least one flow controller, at least one valve, at least one SCF supply system and at least one process fluid supply system. 4. The equipment assembly of claim 2 , wherein an in-line sensor is independently selected at each occurrence from the group consisting of spectrophotometric sensor, particle size sensor, pressure sensor, temperature sensor, infrared sensor, near-infrared sensor, and ultraviolet sensor. 5. The equipment assembly of claim 1 wherein the disperser comprises: a) a vibratable member; b) a vibrator comprising at least one piezoelectric component; c) a converging or diverging nozzle that generates a standing ultrasonic wave during operation; d) a conduit for process fluid and a conduit for SCF; e) a capillary nozzle; and/or f) a vibrator and vibratable member. 6. The equipment assembly of claim 5 , wherein the vibratable member is a nozzle, plate or mesh. 7. The equipment assembly of claim 1 , wherein, for the harvesting filter: a) the process cavity is vertically oriented along its lengthwise axis; b) at least one inlet port is configured to serve as an outlet port for a gaseous particle suspension; c) the porous element and the housing are cylindrical; d) the temperature controller comprises a heating and/or cooling jacket surrounding the housing; e) the geometry of the conical portion is such that the upper wider end has a diameter of about 25 to about 125 mm, the lower narrower end has a diameter of about 5 to about 50 mm and the conical portion is about 50 to about 250 mm in length; f) the process cavity further comprises a linear cylindrical portion in which the porous element is disposed; g) the spacing between the outer surface of the porous element and the inner surface of the process cavity is in the range of about 5 to about 100 mm; h) the outlet port is configured as reversible-flow port to serve as an outlet for liquid and an inlet for gas; i) the diameter of the inner conduit is in the range of about 5 to about 60 mm; j) the outer diameter of the porous element is in the range of about 10 to about 60 mm; k) the system further comprises one or more valves that direct flow of a liquid particle suspension to the harvesting filter and direct flow of a gaseous particle suspension from the harvesting filter; l) the high pressure filter and precipitation chamber are adapted to operate at about 800 to about 3000 psi; m) a portion of the process cavity of the filter housing is cylindrical, rectangular, ellipsoidal or spherical; n) the porous element is disposed within the process cavity such that its surface is tangential to, perpendicular to or at a non-perpendicular angle with respect to the linear axis of the housing or with respect to the overall flow of fluid across or through the surface of the porous element; o) the porous element comprises substantially the same porosity throughout; p) the porous element comprises a first porous portion and a second porous portion, wherein the average diameter of the pores of the first portion is greater than the average diameter of the pores of the second portion; q) the porous element comprises two substantially coextensive porous portions differing in the average diameter of their respective pores; r) a first porous portion of the porous element has an average pore diameter of about 0.3-0.6 microns, and a second porous portion of the porous element has an average pore diameter of about 0.02-0.10 microns; s) the porous element can be a tube or plate; t) a portion of the porous element is a lamina and the porous element comprises two or more laminas; u) the high pressure filter comprises one, two, three, four or plural porous elements; v) the porous element is conductively engage with the upper portion of the filter assembly; w) the porous element is conductively engaged with the lower portion of the filter assembly; x) one or more porous elements together occupy up to about 90% of the volume of the process cavity of the filter assembly; and/or y) the filter housing and/or porous element is invertible. 8. The equipment assembly of claim 7 , wherein the vertical orientation is perpendicular to the ground or parallel to the linear axis of a plumb bob line. 9. The equipment assembly of claim 1 , wherein the low pressure particle collection filter system comprises: a low pressure housing defining a lengthwise process cavity and comprising at least one inlet port, at least one gas outlet port and at least one particle outlet p
Use of anti-solvent · CPC title
controlling the pressure · CPC title
Nozzle-type elements (nozzle-type reactors B01J19/26) · CPC title
by filtration · CPC title
by indirect heat exchange · CPC title
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