US3922250A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Late addition of alkali metal sulfonate dye receptivity additive in polyesterification process
Assignee: Phillips Petroleum Co
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Filing: 1974-09-03
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Granted: 1975-11-25
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Expires: 1994-09-03
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)
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 |