Continuous Solid-State Polymerisation Device and Method
US-2016144337-A1 · May 26, 2016 · US
US9649617B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9649617-B2 |
| Application number | US-201314902076-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 21, 2013 |
| Priority date | Jul 10, 2013 |
| Publication date | May 16, 2017 |
| Grant date | May 16, 2017 |
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A continuous solid-state polymerization device according to the present invention comprises: a feeder for injecting a prepolymer continuously; a transverse reactor connected to the feeder via a first connector to receive the prepolymer from the feeder and to perform solid-state polymerization, the reactor itself rotating; and a chamber connected to the transverse reactor via a second connector to receive a polymer, which has been discharged from the transverse reactor, and solid-state polymerization of which has been completed, and to discharge the polymer, wherein the transverse reactor has a demolding coating film formed on the inner wall thereof, and the feeder, the transverse reactor and the chamber are in a vacuum state. The continuous solid-state polymerization device can prevent formation of an interval, in which the prepolymer stagnates, and can perform solid-state polymerization continuously in a vacuum state without using inert gas.
Opening claim text (preview).
The invention claimed is: 1. A continuous solid-state polymerization apparatus comprising: a feeder for continuously introducing prepolymers; a rotatable transverse reactor connected to the feeder via a first connector and receiving the prepolymers from the feeder to perform solid-state polymerization; a chamber connected to the transverse reactor via a second connector and receiving and discharging solid-state polymerized polymers from the transverse reactor; and a sealing member preventing leakage/inflow of gas and liquid from/into the first and second connectors, wherein the sealing member is a magnetic fluid seal, wherein the transverse reactor has a release coating film formed on an inner wall thereof, and the feeder, the transverse reactor and the chamber are under a vacuum. 2. The continuous solid-state polymerization apparatus according to claim 1 , wherein the release coating film is an organic coating film, an inorganic coating film, or an organic/inorganic hybrid coating film. 3. The continuous solid-state polymerization apparatus according to claim 1 , wherein the release coating film has a thickness of about 1 μm to about 100 μm. 4. The continuous solid-state polymerization apparatus according to claim 1 , wherein a vacuum pump is connected to the chamber. 5. The continuous solid-state polymerization apparatus according to claim 1 , wherein a vacuum pump is further connected to the feeder. 6. The continuous solid-state polymerization apparatus according to claim 1 , wherein the transverse reactor comprises a pre-heating zone, a main-heating zone, and a cooling zone. 7. The continuous solid-state polymerization apparatus according to claim 1 , further comprising: a first hopper receiving the prepolymers from outside and maintained at atmospheric pressure; and a second hopper connected to the first hopper and receiving the prepolymers from the first hopper under atmospheric pressure and transferring the prepolymers to the feeder under a vacuum. 8. The continuous solid-state polymerization apparatus according to claim 1 , further comprising: a third hopper connected to the chamber and receiving the polymers from the chamber under a vacuum and discharging the polymers outside under atmospheric pressure. 9. The continuous solid-state polymerization apparatus according to claim 1 , wherein the transverse reactor further has protrusions on the inner wall thereof. 10. The continuous solid-state polymerization apparatus according to claim 1 , wherein the prepolymer is a polymer having an inherent viscosity (IV) of about 0.09 dL/g to about 0.49 dL/g. 11. The continuous solid-state polymerization apparatus according to claim 1 , the solid-state polymerized polymer has an inherent viscosity (IV) of about 0.5 dL/g to about 1.5 dL/g. 12. A solid-state polymerization method using the continuous solid-state polymerization apparatus according to claim 1 , the method comprising: introducing the prepolymers into the feeder; solid-state polymerizing the introduced prepolymers in the transverse reactor; and discharging the solid-state polymerized polymers to the chamber, wherein the above steps are continuously performed. 13. The solid-state polymerization method according to claim 12 , wherein the solid-state polymerization is performed under a pressure of about 0.1 torr to about 100 torr.
of synthetic organic material · CPC title
comprising coatings on the surfaces in direct contact with the reactive components · CPC title
Solid state polycondensation · CPC title
controlling the pressure · CPC title
Cross-Sectional Technologies · mapped topic
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