Device for preparation of expanded microspheres
View Patent ↗A device includes a heating zone having an inlet, and an outlet, a pump upstream of and in fluid communication with the heating zone, and capable of generating above-atmospheric pressure in the heating zone; an element for heating the heating zone; an expansion zone with an inlet and an outlet, said inlet of the expansion zone being connected to the outlet of the heating zone in such a way that a pressure drop is created, such that the expansion zone is at a lower pressure than the heating zone; and a back pressure generator downstream of the expansion zone configured to create a variable counter pressure in the expansion zone.
1. A device for expanding unexpanded, thermally expandable, thermoplastic microspheres, comprising:
a heating zone having an inlet, and an outlet;
a pump upstream of and in fluid communication with the heating zone for feeding a slurry of unexpanded, thermally expandable, thermoplastic microspheres into the heating zone, wherein the pump is capable of generating above-atmospheric pressure in the heating zone;
an element for heating the heating zone to soften the microspheres fed into the heating zone;
an expansion zone with an inlet and an outlet, said inlet of the expansion zone being connected to the outlet of the heating zone in such a way that a pressure drop is created across the expansion zone inlet, such that a pressure in the expansion zone is at a lower pressure than the heating zone for expanding the microspheres in the expansion zone;
a distribution pipe located downstream of the expansion zone with a first inlet in fluid communication with the outlet of the expansion zone, a second inlet configured to be fluidly coupled to a cooling medium source and an outlet; and
an adjustable back pressure generator disposed in the distribution pipe for creating a variable counter pressure to influence the pressure in the expansion zone.
2. A device according to claim 1 , wherein the element for heating is configured to heat the slurry passing through the heating zone without direct contact with any fluid heat transfer medium.
3. A device according to claim 2 , wherein the back pressure generator is a flow restriction adjuster placed after the outlet of the expansion zone and operable to adjust a volume flow per unit pressure drop in the expansion zone.
4. A device according to claim 2 , wherein the back pressure generator comprises a flow adjuster for adjusting the flow of cooling medium through the distribution pipe.
5. A device according to claim 1 , wherein the back pressure generator is a flow restriction adjuster placed after the outlet of the expansion zone and operable to adjust a volume flow per unit pressure drop in the expansion zone.
6. A device according to claim 1 , wherein the back pressure generator comprises a flow adjuster for adjusting the flow of cooling medium through the distribution pipe.
7. A process for expanding unexpanded, thermally expandable, thermoplastic microspheres comprising a thermoplastic polymer encapsulating a blowing agent, wherein said blowing agent is a liquid having a boiling temperature not higher than the softening temperature of the thermoplastic polymer shell, the process comprising:
feeding a slurry of unexpanded, thermally expandable, thermoplastic microspheres into a heating zone by a pump capable of generating higher than atmospheric pressure in the heating zone,
heating the microspheres to a temperature above their softening temperature, while under a pressure sufficiently high to ensure they do not fully expand;
passing the so-heated microspheres from the heating zone to an expansion zone, such that a pressure drop is created, resulting in a pressure in the expansion zone sufficiently low for the microspheres to expand, and
removing the expanded microspheres from the expansion zone,
wherein the expansion zone is configured to create a variable counter pressure by a back-pressure generator downstream of the expansion zone.
8. A process as claimed in claim 7 , in which the pressure maintained in the heating zone is from about 10 to about 50 bars.
9. A process as claimed in claim 8 , in which the temperature of the slurry in the heating zone is from about 60° C. to about 250° C.
10. A process as claimed in claim 7 , in which the temperature of the slurry in the heating zone is from about 60° C. to about 250° C.
11. A process as claimed in claim 7 , in which the expansion zone is connected to a downstream outlet pipe, and said outlet pipe flows into a downstream distribution pipe through a connection, said distribution pipe also having an inlet for cooling medium, upstream of the connection, wherein the a flow of cooling medium is fed to the inlet of the distribution pipe.
12. A process as claimed in claim 11 , in which the cooling medium a flow of gas, liquid or particles that are inert to the expanded thermoplastic microspheres.
13. A process as claimed in claim 12 , in which the cooling medium is selected from air, water, nitrogen, chalk particles, calcium carbonate particles, silica particles, clay particles and TiO 2 particles, or any combination thereof.
14. A process according to claim 7 , in which the unexpanded thermally expandable, thermoplastic microspheres are fed to a device.
15. A device for processing unexpanded, thermally expandable, thermoplastic microspheres into an expanded form, the device comprising:
a heater having a heater inlet, a heater outlet, and a heating zone therebetween;
a pump in fluid communication with the heater inlet for feeding a slurry of unexpanded, thermally expandable, thermoplastic microspheres into the heating zone at a first pressure condition sufficiently elevated about atmospheric pressure to prevent full expansion of the microspheres in a softened state;
a heating element thermally coupled to the heating zone for heating the microspheres to the softened state;
an expander having an expander inlet in fluid communication with the heater outlet, an expander outlet, and an expansion zone therebetween, wherein a pressure drop is created across the expander inlet and the expansion zone is at a second pressure condition that is lower than the first pressure condition for expanding the microspheres in the expansion zone; and
a distribution pipe located downstream of the expansion zone having a first inlet in fluid communication with the expander outlet, a second inlet fluidly coupled to a cooling medium source and an outlet; and
an adjustable back pressure generator disposed in the distribution pipe for creating a variable counter pressure to influence the pressure in the expansion zone.
16. The device of claim 15 wherein the cooling medium source comprises a cooling medium that is inert to the expanded thermoplastic microspheres.
17. A device according to claim 15 , wherein the back pressure generator is a flow restriction adjuster placed after the outlet of the expander and operable to adjust a volume flow per unit pressure drop in the expansion zone.