Process for devolatilization

• US 5,932,691 A
• Filed: 12/05/1997
• Issued: 08/03/1999
• Est. Priority Date: 12/05/1997
• Status: Expired due to Fees

• Current Assignee: Union Carbide Chemicals & Plastics Technology Corporation (Dow, Inc.)
• Original Assignee: Union Carbide Chemicals & Plastics Technology Corporation (Dow, Inc.)
• Inventors: Khanin, David, Scarola, Leonard Sebastian
• Primary Examiner(s): TESKIN, FRED M
• Application Number:
  US08/985,796
• Time in Patent Office: 606 Days
• Field of Search: 528/483, 528/492, 528/501, 528/502 R, 528/503, 264/102, 264/345, 521/79
• US Class Current: 528/483
• CPC Class Codes: B29B 7/847 Removing of gaseous components before or after mixing

Abstract

A process for the devolatilization of a thermoplastic polymer containing gaseous impurities in an apparatus having a melting zone, a mixing zone, and a reduced pressure zone, comprising:

(a) (i) adding a granular blowing agent directly or via a masterbatch to the polymer prior to the introduction of the polymer into the melting zone, said blowing agent being added in an amount of about 1 to about 4 percent by weight based on the weight of the polymer or (ii) adding a gaseous blowing agent to the mixing zone;

(b) melting the polymer in the melting zone;

(c) mixing the molten polymer and blowing agent in the mixing zone under sufficient pressure to maintain the blowing agent in the mixture;

(d) at a temperature sufficient for decomposition or expansion, (i) decomposing the granular blowing agent in the mixing zone and/or in the reduced pressure zone or (ii) expanding the gaseous blowing agent in the reduced pressure zone wherein the blowing agent in its decomposed or expanded state develops froth cells in the molten polymer;

(e) in the reduced pressure zone, reducing the pressure at the surface of the molten polymer in a sufficient amount to remove essentially all of the gaseous impurities;

(f) optionally, repeating steps (c), (d), and (e) at least once; and

(g) recovering the polymer in an essentially unfoamed state.

Claims

1. A process for the devolatilization of a thermoplastic polymer containing gaseous impurities in an apparatus having a melting zone, a mixing zone, and a reduced pressure zone, comprising:

(a) adding a gaseous blowing agent to the mixing zone;

(b) melting the polymer in the melting zone;

(c) mixing the molten polymer and blowing agent in the mixing zone under sufficient pressure to maintain the blowing agent in the mixture;

(d) at a temperature sufficient for expansion, expanding the gaseous blowing agent in the reduced pressure zone wherein the blowing agent in its expanded state develops froth cells in the molten polymer;

(e) in the reduced pressure zone, reducing the pressure at the surface of the molten polymer in a sufficient amount to remove essentially all of the gaseous impurities;

(f) optionally, repeating steps (c), (d), and (e) at least once; and

(g) recovering the polymer in an essentially unfoamed state.

2. The process defined in claim 1 wherein step (a) is carried out by adding a gaseous blowing agent to the mixing zone through a porous element.

3. The process defined in claim 1 wherein, in step (c), the pressure is in the range of about 300 to about 800 psia.

4. The process defined in claim 1 wherein, in step (e), the pressure is reduced to at least 0.1 psia or less.

5. The process defined in claim 1 wherein, in step (f), steps (c), (d), and (e) are repeated at least once.

6. A process for the devolatilization of a thermoplastic polymer containing gaseous impurities in an apparatus having a melting zone, a mixing zone, and a reduced pressure zone, comprising

(a) adding a gaseous blowing agent, nitrogen, to the mixing zone at a pressure in the range of about 20 to about 50 percent above the melt pressure

(b) melting the polymer in the melting zone;

(c) mixing the molten polymer and blowing agent in the mixing zone under a pressure of about 300 to about 500 psia

(d) at a temperature sufficient for expansion, about 120 to about 270 degrees C., expanding the gaseous blowing agent in the reduced pressure zone wherein the blowing agent in its expanded state develops froth cells in the molten polymer;

(e) in the reduced pressure zone, reducing the pressure at the surface of the molten polymer to 0.1 psia or less to remove essentially all of the gaseous impurities;

(f) repeating steps (c), (d), and (e), 2 to 4 times; and

(g) recovering the polymer in an essentially unfoamed state.