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US4395536A Expired / Lapsed US ⏱️ 0.0 years remaining

Preparation of aromatic copolyesters via in situ esterification with isopropenyl esters of an alkyl acid

Assignee: Celanese Corp
•
Filing: 1981-11-17
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Granted: 1983-07-26
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Expires: 2001-11-17
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Abstract

Abstract Provided is a method for preparing aromatic copolyesters involving in situ esterification with an isopropenyl ester of an alkyl acid, e.g., isopropenyl acetate. The process comprises reacting the aromatic hydroxy monomers with an isopropenyl ester of an alkyl acid such as isopropenyl acetate in a polymerization vessel in order to esterify the hydroxy moieties, and then polymerizing the esterified hydroxy monomers with aromatic carboxylic acid monomers in the resultant esterification reaction medium to form the aromatic copolyester. Both the esterification and polymerization reactions can be effectively conducted in the same vessel without having to separate out and/or transfer the esterification products from a separate vessel as the polyester polymerization is conducted in the esterification reaction mixture. The esterification is generally carried out in the presence of an acid esterification catalyst, which is preferably neutralized upon completion of the esterification reaction with a suitable basic neutralizing agent, e.g., barium hydroxide.

Inventors

  • 👤 Larry F. Charbonneau

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 11:54
CPC Classifications
C; C08; C08G; C08G63/00; C08G63/02; C08G63/60; C08G63/605; C08G63/06; C08G63/065

Claims Analysis

Total Claims: 42
Claim 1
Independent Claim 57 words
A process for preparing an aromatic polyester comprising: (i) reacting at least one aromatic hydroxy moiety containing compound with an isopropenyl ester of an alkyl acid under esterification, reaction conditions, and (ii) reacting the esterified compounds with at least one aromatic acid moiety containing compound in the resultant esterification reaction mixture of (i) under polyester polymerization conditions.
Claim 2
Dependent Claim 57 words
A process for preparing an aromatic polyester comprising: (i) reacting at least one aromatic hydroxy moiety containing compound with an isopropenyl ester of an alkyl acid under esterification, reaction conditions, and (ii) reacting the esterified compounds with at least one aromatic acid moiety containing compound in the resultant esterification reaction mixture of (i) under polyester polymerization conditions.
Claim 3
Dependent Claim 44 words
The process of claim 1 wherein isopropenyl acetate is reacted with at least one aromatic hydroxy moiety containing compound under acetylation reaction conditions, and then reacting the acetylated compounds with at least one aromatic acid moiety containing compound in the resultant acetylation reaction mixture.
Claim 4
Dependent Claim 15 words
The process of claim 2 wherein the aromatic acid is present during the acetylation reaction.
Claim 5
Dependent Claim 30 words
The process of claim 2 or 3 wherein at least one of the aromatic acid moiety containing compounds is also at least one of the aromatic hydroxy moiety containing compounds.
Claim 6
Dependent Claim 22 words
The process of claim 2 wherein the acetylation reaction is conducted in the presence of a catalytic amount of an acetylation catalyst.
Claim 7
Dependent Claim 35 words
The process of claim 5 wherein the acetylation catalyst is a strong acid catalyst selected from the group consisting of p-toluenesulfonic acid, sulfosalicylic acid, methanesulfonic acid, hydrogen chloride, hydrogen bromide, perchloric acid and sulfuric acid.
Claim 8
Dependent Claim 20 words
The process of claim 6 wherein said catalyst is selected from the group consisting of p-toluenesulfonic acid and methanesulfonic acid.
Claim 9
Dependent Claim 29 words
The process of claim 6 wherein a basic neutralizing agent is added to the acetylation reaction mixture upon termination of the acetylation in order to neutralize the acid catalyst.
Claim 10
Dependent Claim 13 words
The process of claim 8 wherein said basic neutralizing agent is metallic hydroxide.
Claim 11
Dependent Claim 14 words
The process of claim 8 or 9 wherein the neutralizing agent is barium hydroxide.
Claim 12
Dependent Claim 27 words
The process of claim 2 wherein the reaction temperature of the acetylation step (i) is in the range of from about 60° C. to about 130° C.
Claim 13
Dependent Claim 30 words
The process of claim 2 wherein the reaction temperature is raised to a temperature in the range of from about 180° to 350° C. upon initiation of the polymerization (ii).
Claim 14
Dependent Claim 26 words
The process of claim 2 wherein the reaction temperture during the polymerization step (ii) is in the range of from about 225° to about 350° C.
Claim 15
Dependent Claim 24 words
The process of claim 2 wherein the polyester polymerization reaction (ii) is conducted in the presence of a catalytic amount of a polymerization catalyst.
Claim 16
Dependent Claim 16 words
The process of claim 2 wherein the polymerization reaction (ii) is conducted under melt polymerization conditions.
Claim 17
Dependent Claim 23 words
The process of claim 2 wherein an hydroxy benzoic acid is employed as an aromatic hydroxy moiety containing compound and an aromatic acid.
Claim 18
Dependent Claim 11 words
The process of claim 16 wherein p-hydroxy benzoic acid is employed.
Claim 19
Dependent Claim 20 words
The process of claim 2 wherein the isopropenyl acetate is reacted in (i) with p-hydroxy benzoic acid and 6-hydroxy-2-naphthoic acid.
Claim 20
Dependent Claim 23 words
The process of claim 18 wherein the aromatic acid moiety containing compound of (ii) comprises the acetylated p-hydroxy benzoic acid and 6-hydroxy-2-naphthoic acid.
Claim 21
Dependent Claim 23 words
The process of claim 2 wherein the isopropenyl acetate is reacted with p-hydroxy benzoic acid, 6-hydroxy-2-naphthoic acid and an aromatic diol in (i).
Claim 22
Dependent Claim 11 words
The process of claim 20 wherein said aromatic diol comprises hydroquinone.
Claim 23
Dependent Claim 16 words
The process of claim 20 wherein aromatic acid of (ii) is comprised of an aromatic diacid.
Claim 24
Dependent Claim 12 words
The process of claim 22 wherein the aromatic diacid is terephthalic acid.
Claim 25
Dependent Claim 18 words
The process of claim 2 wherein the aromatic-hydroxy moiety containing compound is comprised of a hydroxy naphthoic acid.
Claim 26
Dependent Claim 13 words
The process of claim 24 wherein the hydroxy naphthoic acid is 6-hydroxy-2-naphthoic acid.
Claim 27
Dependent Claim 22 words
The process of claim 24 wherein the isopropenyl acetate is reacted with a hydroxy naphthoic acid and an aromatic diol in (i).
Claim 28
Dependent Claim 11 words
The process of claim 26 wherein said aromatic diol is hydroquinone.
Claim 29
Dependent Claim 17 words
The process of claim 26 wherein the aromatic acid of (ii) is comprised on an aromatic diacid.
Claim 30
Dependent Claim 12 words
The process of claim 28 wherein the aromatic diacid is terephthalic acid.
Claim 31
Dependent Claim 70 words
A process for preparing a wholly aromatic polyester comprising reacting a hydroxybenzoic acid and a hydroxy naphthoic acid with an isopropenyl ester of an alkyl acid under esterification reaction conditions to thereby esterify the hydroxy moieties of the hydroxy benzoic acid and hydroxy naphthoic acid and then raising the temperature of the reaction mixture to a temperature sufficient to initiate polymerization and conducting the polymerization under polyester polymerization reaction conditions.
Claim 32
Dependent Claim 70 words
A process for preparing a wholly aromatic polyester comprising reacting a hydroxybenzoic acid and a hydroxy naphthoic acid with an isopropenyl ester of an alkyl acid under esterification reaction conditions to thereby esterify the hydroxy moieties of the hydroxy benzoic acid and hydroxy naphthoic acid and then raising the temperature of the reaction mixture to a temperature sufficient to initiate polymerization and conducting the polymerization under polyester polymerization reaction conditions.
Claim 33
Dependent Claim 16 words
The process of claim 30 wherein the isopropenyl ester of an alkyl acid is isopropenyl acetate.
Claim 34
Dependent Claim 45 words
The process of claim 31 wherein the acetylation is conducted at a temperature in the range of from about 60° C. to about 130° C. and the polymerization is conducted at a temperature in the range of from about 180° C. to about 350° C.
Claim 35
Dependent Claim 87 words
The process of claim 31 wherein p-hydroxybenzoic acid and 6-hydroxy-2-naphthoic acid are reacted with isopropenyl acetate at a temperature in the range of from about 60° C. to about 130° C. in the presence of an acid catalyst until acetylation is completed, adding a basic reagent in an amount sufficient to neutralize the acid catalyst and then raising the reaction temperature to a temperature sufficient to initiate polymerization and conducting the polymerization at a temperature in the range of from about 250° C. to about 350° C.
Claim 36
Dependent Claim 28 words
The process of claim 33 wherein the acid catalyst is selected from the group consisting of methanesulfonic acid and p-toluenesulfonic acid and the basic reagent is barium hydroxide.
Claim 37
Dependent Claim 49 words
A process for preparing an aromatic polyester comprising heating at least one aromatic hydroxy compound and at least one aromatic acid compound in the presence of an isopropenyl ester of an alkyl acid at an esterification temperature and then at a polymerization temperature to thereby form the aromatic polyester.
Claim 38
Dependent Claim 49 words
A process for preparing an aromatic polyester comprising heating at least one aromatic hydroxy compound and at least one aromatic acid compound in the presence of an isopropenyl ester of an alkyl acid at an esterification temperature and then at a polymerization temperature to thereby form the aromatic polyester.
Claim 39
Dependent Claim 16 words
The process of claim 35 wherein the isopropenyl ester of an alkyl acid is isopropenyl acetate.
Claim 40
Dependent Claim 31 words
The process of claim 36 wherein an acid acetylation catalyst is employed and a basic reagent is added upon completion of acetylation in an amount sufficient to neutralize the acid catalyst.
Claim 41
Dependent Claim 12 words
The process of claim 37 wherein the basic reagent is barium hydroxide.
Claim 42
Dependent Claim 46 words
The process of claim 1, wherein the aromatic hydroxy moiety containing compound comprises at least one of an aromatic diol or aromatic hydroxy acid, and the aromatic acid moiety containing compound comprises at least one of an aromatic diacid, or aromatic hydroxy acid or derivative thereof.

References Cited (Backward Citations)

US3637595A Cited
US4316004A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1986-07-25 1987-01-24 1987-07-26 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1990-07-25 1991-01-24 1991-07-26 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1994-07-25 1995-01-24 1995-07-26 $7700.00 Window Closed / Lapsed

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