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US3922250A Expired / Lapsed US ⏱️ 0.0 years remaining

Late addition of alkali metal sulfonate dye receptivity additive in polyesterification process

Assignee: Phillips Petroleum Co
•
Filing: 1974-09-03
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Granted: 1975-11-25
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Expires: 1994-09-03
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Abstract

Abstract In a polyesterification process, a suitable ester-forming sulfonate dyeability modifier is introduced into the reaction zone after the initial esterification or transesterification reaction is essentially complete.

Inventors

  • 👤 James W Cleary

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 03:32
CPC Classifications
C; C08; C08G; C08G63/00; C08G63/68; C08G63/688; C08G63/6884; C08G63/6886

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 37 words
IN A POLYESTERIFICATION PROCESS COMPRISING CONTACTING A DICARBOXYLIC ACID OR ITS ESTER-FORMING DERIVATIVE AND A DIOL UNDER POLYESTER-FORMING CONDITIONS, THE IMPROVEMENT COMPRISING ADDING AN EFFECTIVE DYE RECEPTIVITY IMPROVING AMOUNT OF A SULFONATE COMPOUND HAVING THE GENERAL FORMULA
Claim 2
Dependent Claim 37 words
IN A POLYESTERIFICATION PROCESS COMPRISING CONTACTING A DICARBOXYLIC ACID OR ITS ESTER-FORMING DERIVATIVE AND A DIOL UNDER POLYESTER-FORMING CONDITIONS, THE IMPROVEMENT COMPRISING ADDING AN EFFECTIVE DYE RECEPTIVITY IMPROVING AMOUNT OF A SULFONATE COMPOUND HAVING THE GENERAL FORMULA
Claim 3
Dependent Claim 35 words
In a polyesterification process comprising contacting a dicarboxylic acid or its ester-forming derivative and a diol under polyester forming conditions, the improvement comprising incorporating into said polyesterification process a sulfonate represented by the general formula
Claim 4
Dependent Claim 35 words
In a polyesterification process comprising contacting a dicarboxylic acid or its ester-forming derivative and a diol under polyester forming conditions, the improvement comprising incorporating into said polyesterification process a sulfonate represented by the general formula
Claim 5
Dependent Claim 13 words
A process according to claim 2 wherein said sulfonate is a mixture of
Claim 6
Dependent Claim 13 words
A method according to claim 2 wherein said sulfonate is a mixture of
Claim 7
Dependent Claim 14 words
A method accorDing to claim 2 wherein said sulfonate is represented by the formula
Claim 8
Dependent Claim 10 words
A process according to claim 2 wherein said sulfonate is
Claim 9
Dependent Claim 44 words
A method according to claim 2 wherein said sulfonate is selected from the group consisting of dimethyl sodium 5-sulfoisophthalate, dimethyl potassium 5-sulfoisophthalate, di-n-pentyl lithium 3-sulfoterephthalate, potassium 5-sulfoisophthalic acid, monosodium 5-sulfosalicylic acid, monopotassium 5-sulfosalicylic acid, methyl lithium 5-sulfosalicylate, n-propyl sodium 3-hydroxy-4-sulfobenzoate, and monopotassium 2,5-dimethyl-4-hydroxy-3-sulfobenzoic acid.
Claim 10
Dependent Claim 19 words
A method according to claim 2 wherein said sulfonate is selected from dimethyl sodium 5-sulfoisophthalate and monosodium 5-sulfosalicylic acid.
Claim 11
Dependent Claim 36 words
A method according to claim 2 wherein said dicarboxylic acid or its ester-forming derivative is an ester of an aromatic dicarboxylic acid and said diol is a glycol containing two to 10 carbon atoms per molecule.
Claim 12
Dependent Claim 18 words
A method according to claim 9 wherein said ester is dimethyl terephthalate and said glycol is ethylene glycol.
Claim 13
Dependent Claim 14 words
A method according to claim 10 wherein said alkali metal hydroxide is sodium hydroxide.
Claim 14
Dependent Claim 99 words
A method according to claim 11 wherein said dimethyl terephthalate and said ethylene glycol are heated at a temperature of 150* C. to 270* C. to effect an initial transesterification reaction with removal of the methyl alcohol thus evolved; and thereafter the reaction mixture is further heated to complete the polycondensation and to distill excess glycol from the reaction mixture, the initial molar ratio of glycol to terephthalate being in the range of 2:1 to 4:1, there being present during said polyesterification a catalyst selected from the group consisting of antimony oxide, zinc acetate, manganese acetate, and cobaltous acetate.

References Cited (Backward Citations)

US3018272A Cited
US3033824A Cited
US3528947A Cited
US3663508A Cited
US3634541A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-11-24 1979-05-26 1979-11-25 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-11-24 1983-05-26 1983-11-25 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-11-24 1987-05-26 1987-11-25 $7700.00 Window Closed / Lapsed

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