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US4073773A Expired / Lapsed US ⏱️ 0.0 years remaining

Melt polymerization method for making polyetherimides

Assignee: General Electric Co
•
Filing: 1976-12-30
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Granted: 1978-02-14
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Expires: 1996-12-30
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Abstract

Abstract An improved extrusion melt polymerization method for continuously making polyetherimides is disclosed wherein a mixture of an organic diamine and an aromatic bis(ether anhydride) is continuously fed through an inlet opening into a screw extruder having a second opening downstream from the inlet opening. The mixture is passed through a first extruder zone maintained at a low temperature to a zone where the mixture is melted and water of reaction is continuously removed through the second opening. A melt seal may be employed between the second opening and a third opening through which water of reaction may be removed under vacuum.

Inventors

  • 👤 Eugene G. Banucci
  • 👤 Gary A. Mellinger

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 21:42
CPC Classifications
C; C08; C08G; C08G73/00; C08G73/06; C08G73/10; C08G73/1067; C08G73/1071; B; B01; B01J; B01J19/00; B01J19/18; B01J19/20; B29; B29C; B29C48/00; B29C48/25; B29C48/36; B29C48/50; B29C48/76; C08G73/1003; C08G73/1007; C08G73/1028; C08G73/1046; C08G73/1053; B29C48/03; B29C48/06

Claims Analysis

Total Claims: 17
Claim 1
Independent Claim 245 words
In an extrusion melt polymerization method for making polyetherimides wherein a reaction mixture containing as essential ingredients (I) an organic diamine of the formula, H.sub.2 NR.sup.1 NH.sub.2 and (II) an aromatic bis(ether anhydride) of the formula, ##STR9## and (I) is present in an amount of 0.5 to 2.0 moles per mole of (II), is continuously fed through an inlet opening into a screw extruder having a barrel maintained at melt polymerization temperatures and water of reaction is continuously vented from the extruder, where R is a divalent aromatic organic radical having from 6 to 30 carbon atoms, R 1 is a divalent organic radical selected from the group consisting of said R radicals, alkylene radicals having from 2 to about 20 carbon atoms, cycloalkylene radicals, and C.sub.(2-8) alkylene terminated polydiorganosiloxane radicals, the improvement comprising: (A) using a screw extruder having a second opening through the extruder wall and having an outlet orifice, said second opening being in a second barrel zone intermediate said inlet opening and said orifice, said second barrel zone being maintained at melt polymerization temperature; (B) continuously conveying the reaction mixture through a first barrel zone maintained at a temperature below the melting point of the lowest melting essential ingredient, said first barrel zone extending from said inlet opening to said second barrel zone; and (C) continuously venting water of reaction at a temperature of up to 400° C through said second opening while continuously feeding reaction mixture through said inlet opening.
Claim 2
Dependent Claim 245 words
In an extrusion melt polymerization method for making polyetherimides wherein a reaction mixture containing as essential ingredients (I) an organic diamine of the formula, H.sub.2 NR.sup.1 NH.sub.2 and (II) an aromatic bis(ether anhydride) of the formula, ##STR9## and (I) is present in an amount of 0.5 to 2.0 moles per mole of (II), is continuously fed through an inlet opening into a screw extruder having a barrel maintained at melt polymerization temperatures and water of reaction is continuously vented from the extruder, where R is a divalent aromatic organic radical having from 6 to 30 carbon atoms, R 1 is a divalent organic radical selected from the group consisting of said R radicals, alkylene radicals having from 2 to about 20 carbon atoms, cycloalkylene radicals, and C.sub.(2-8) alkylene terminated polydiorganosiloxane radicals, the improvement comprising: (A) using a screw extruder having a second opening through the extruder wall and having an outlet orifice, said second opening being in a second barrel zone intermediate said inlet opening and said orifice, said second barrel zone being maintained at melt polymerization temperature; (B) continuously conveying the reaction mixture through a first barrel zone maintained at a temperature below the melting point of the lowest melting essential ingredient, said first barrel zone extending from said inlet opening to said second barrel zone; and (C) continuously venting water of reaction at a temperature of up to 400° C through said second opening while continuously feeding reaction mixture through said inlet opening.
Claim 3
Dependent Claim 21 words
The method of claim 1, further including maintaining the first and second barrel zones only partially filled with the reaction mixture.
Claim 4
Dependent Claim 37 words
The method of claim 2, wherein the extruder includes a third barrel zone intermediate said second zone and said outlet orifice, and further including maintaining said third barrel zone substantially filled and sealed with the reaction mixture.
Claim 5
Dependent Claim 45 words
The method of claim 3, wherein the extruder has a third opening through the extruder wall, said third opening being in a fourth barrel zone intermediate said third zone and said orifice, and continuously venting water of reaction through said third opening under applied vacuum.
Claim 6
Dependent Claim 12 words
The method of claim 1, wherein the extruder includes two intermeshing screws.
Claim 7
Dependent Claim 12 words
The method of claim 2, wherein the extruder includes two intermeshing screws.
Claim 8
Dependent Claim 39 words
The method of claim 4, wherein the extruder includes a screw having first direction flights in said first, second and fourth zones and having second direction flights in said third zone, said first direction being opposite and second direction.
Claim 9
Dependent Claim 19 words
The method of claim 4, wherein the extruder includes a screw having a kneading block in said third zone.
Claim 10
Dependent Claim 31 words
The method of claim 1, where the aromatic bis(ether anhydride) has the formula, ##STR10## where R 4 is ##STR11## and Q' is a member selected from the class consisting of ##STR12##
Claim 11
Dependent Claim 14 words
The method of claim 9, where the aromatic bis(ether anhydride) has the formula, ##STR13##
Claim 12
Dependent Claim 14 words
The method of claim 9, where the aromatic bis(ether anhydride) has the formula, ##STR14##
Claim 13
Dependent Claim 14 words
The method of claim 9, where the aromatic bis(ether anhydride has the formula, ##STR15##
Claim 14
Dependent Claim 17 words
The method of claim 1, wherein the dianhydride is 2,2-bis 4-(3,4-dicarboxyphenoxy)phenyl!-propane dianhydride and the diamine is m-phenylenediamine.
Claim 15
Dependent Claim 17 words
The method of claim 1, wherein the dianhydride is 2,2-bis 4-(3,4-dicarboxyphenoxy)phenyl!propane dianhydride and the diamine is 4,4'-methylenedianiline.
Claim 16
Dependent Claim 17 words
The metho of claim 1, wherein the dianhydride is 2,2-bis 4-(2,3-dicarboxyphenoxy)phenyl!propane dianhydride and the diamine is m-phenylenediamine.
Claim 17
Dependent Claim 17 words
The method of claim 1, wherein the dianhydride is 2,2-bis 4-(2,3-dicarboxyphenoxy)phenyl!propane dianhydride and the diamine is 4,4'-methylenedianiline.

References Cited (Backward Citations)

US3803085A Cited
US3833546A Cited
US4011198A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1981-02-13 1981-08-15 1982-02-14 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1985-02-13 1985-08-15 1986-02-14 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1989-02-13 1989-08-15 1990-02-14 $7700.00 Window Closed / Lapsed

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