Polymer flake degassing system and methods
AssigneeChevron Phillips Chemical Company LP
InventorsKenneth A. Dooley, Jeffrey S. Lowell, Joseph Curren
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Abstract
Systems and methods for improved degassing of polymer flake are provided herein. These systems include a polymerization reactor configured to polymerize one or more olefin monomers and produce a product stream comprising solid polymer flake entrained in a fluid; a flash chamber configured to separate the solid polymer flake from the fluid and to produce a fluid stream and a concentrated stream; and a first degassing chamber configured to separate the concentrated stream by contacting the concentrated stream with a purge fluid comprising one or more light hydrocarbons to produce a partially degassed polymer flake stream and a purge fluid stream.
Claims20
A system for polymerizing one or more olefin monomers, comprising:
- a polymerization reactor configured to polymerize one or more olefin monomers and produce a product stream comprising solid polymer flake entrained in a fluid;
- a flash chamber configured to separate the solid polymer flake from the fluid and to produce a fluid stream and a concentrated stream, wherein the fluid stream comprises the solid polymer flake in a lower concentration than in the product stream, and wherein the concentrated stream comprises the solid polymer flake in a higher concentration than in the product stream;
- a fluid stream recycle line configured to recycle the fluid stream from the flash chamber to the polymerization reactor;
- a first degassing chamber configured to separate the concentrated stream by contacting the concentrated stream with a first purge fluid comprising one or more light hydrocarbons to produce a partially degassed polymer flake stream and a purge fluid stream, wherein the partially degassed polymer flake stream comprises the fluid in a lower concentration than in the concentrated stream and the purge fluid stream comprises the solid polymer flake in a lower concentration than in the concentrated stream,
- wherein the polymerization reactor, the flash chamber, and the first degassing chamber are distinct from each other.
A process for polymerizing one or more olefin monomers comprising:
- polymerizing one or more olefin monomers in a polymerization reactor to form a product stream comprising solid polymer flake entrained in a fluid;
- passing the product stream to a flash chamber to produce a fluid stream and a concentrated stream of solid polymer flake entrained in the fluid, wherein the fluid stream comprises the solid polymer flake in a lower concentration than in the product stream and the concentrated stream comprises the solid polymer flake in a higher concentration than in the product stream;
- recycling the fluid stream from the flash chamber to the polymerization reactor;
- passing the concentrated stream to a first degassing chamber, wherein a first purge fluid comprising one or more light hydrocarbons contacts the concentrated stream to produce a partially degassed polymer flake stream and a purge fluid stream wherein the partially degassed polymer flake stream comprises the fluid in a lower concentration than in the concentrated stream and the purge fluid stream comprises the solid polymer flake in a lower concentration than in the concentrated stream;
- passing the partially degassed polymer flake stream to a second degassing chamber, wherein a second purge fluid comprising nitrogen contacts the partially degassed polymer flake stream to produce a fully degassed polymer flake stream and a used nitrogen stream, wherein the fully degassed polymer flake stream comprises the fluid at a lower concentration than in the partially degassed polymer flake stream and the used nitrogen stream comprises the solid polymer flake in a lower concentration than in the partially degassed Polymer flake stream,
- wherein a weight ratio of the second purge fluid to the solid polymer flake in the partially degassed polymer flake stream is from about 0.001 to about 0.03.
Dependencies are inferred from the claim text.