US4462947A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Heat-resistant foamed polyesters
Assignee: Mobil Oil AS
•
Filing: 1982-12-28
•
Granted: 1984-07-31
•
Expires: 2002-12-28
Abstract
Abstract There are provided heat-resistant, foamed, crystalline polyesters, such as polyethylene terephthalate foamed with a polycarbonate and subjected to crystallization annealing, which are particularly useful for forming light weight, ovenable food containers.
Inventors
- 👤 Mark T. Huggard
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 23:31
CPC Classifications
C; C08; C08J; C08J9/00; C08J9/04; C08J9/06; C08J9/08; B; B29; B29C; B29C44/00; B29C44/02; B29C44/08; B29C44/34; B29C44/36; B29C44/46; B29C44/50; B29C44/505; B29C44/56; B29C51/00; B29C51/002; B29K; B29K2067/00; B29K2067/003; B29K2105/00; B29K2105/04; B29L; B29L2031/00; B29L2031/712; C08J2367/00; C08J2367/02; Y; Y10; Y10S; Y10S264/00; Y10S264/05
Claims Analysis
Total Claims: 5
Claim 1
Independent Claim
338 words
A process for preparing a thermoformed, foamed, crystalline, high molecular weight linear polyester sheet, said process comprising the steps of: (i) reacting a homogeneous mixture consisting essentially of: (a) a high molecular weight linear polyester, which is a polycondensation product of an aromatic dicarboxylic acid and a glycol; and (b) a high molecular weight linear aromatic polycarbonate represented by the repeating structural unit of the formula: ##STR9## wherein X is a divalent hydrocarbon radical with a total of from 2 up to about 9 carbon atoms selected from the group consisting of ##STR10## in which R 1 represents a member selected from the group consisting of hydrogen and lower alkyl and R 2 represents a member selected from the group consisting of phenyl and alkyl of 1 to 7 carbon atoms, in a weight ratio of (a):(b) of about 20:1 to 1:20, at a temperature and for a period of time sufficient to form the mixture into a softened foamable mass and to release carbon dioxide from said polycarbonate for foaming said mass; (ii) extruding said foamable mass of step (i) into a sheet at a pressure sufficient to cause the released carbon dioxide to expand and reduce the density of the extruded sheet; (iii) cooling said sheet of step (ii) on a chill roll at a temperature from about 70° F. to about 120° F. to inhibit crystallization whereby the average crystallinity of said sheet is in the range from about 0% to about 18%; (iv) contacting said sheet of step (iii) with a mold which is at a temperature in the range of from about 240°-350° F.; (v) applying forces comprising a differential in applied pressure to said sheet of step (iv) so as to make said sheet conform to said mold, whereby a thermoformed sheet is made; (vi) allowing said thermoformed sheet of step (v) to remain in contact with said mold until an average crystallinity of at least about 20% is achieved; and (vii) removing said thermoformed sheet of step (vi) from said mold.
Claim 2
Dependent Claim
338 words
A process for preparing a thermoformed, foamed, crystalline, high molecular weight linear polyester sheet, said process comprising the steps of: (i) reacting a homogeneous mixture consisting essentially of: (a) a high molecular weight linear polyester, which is a polycondensation product of an aromatic dicarboxylic acid and a glycol; and (b) a high molecular weight linear aromatic polycarbonate represented by the repeating structural unit of the formula: ##STR9## wherein X is a divalent hydrocarbon radical with a total of from 2 up to about 9 carbon atoms selected from the group consisting of ##STR10## in which R 1 represents a member selected from the group consisting of hydrogen and lower alkyl and R 2 represents a member selected from the group consisting of phenyl and alkyl of 1 to 7 carbon atoms, in a weight ratio of (a):(b) of about 20:1 to 1:20, at a temperature and for a period of time sufficient to form the mixture into a softened foamable mass and to release carbon dioxide from said polycarbonate for foaming said mass; (ii) extruding said foamable mass of step (i) into a sheet at a pressure sufficient to cause the released carbon dioxide to expand and reduce the density of the extruded sheet; (iii) cooling said sheet of step (ii) on a chill roll at a temperature from about 70° F. to about 120° F. to inhibit crystallization whereby the average crystallinity of said sheet is in the range from about 0% to about 18%; (iv) contacting said sheet of step (iii) with a mold which is at a temperature in the range of from about 240°-350° F.; (v) applying forces comprising a differential in applied pressure to said sheet of step (iv) so as to make said sheet conform to said mold, whereby a thermoformed sheet is made; (vi) allowing said thermoformed sheet of step (v) to remain in contact with said mold until an average crystallinity of at least about 20% is achieved; and (vii) removing said thermoformed sheet of step (vi) from said mold.
Claim 3
Dependent Claim
26 words
A process according to claim 1, wherein said homogeneous mixture of step (i) is heated at a temperature of about 250° C. to about 350° C.
Claim 4
Dependent Claim
24 words
A process according to claim 1, wherein said differential in applied pressure in step (v) is in the range up to about 5 atmospheres.
Claim 5
Dependent Claim
12 words
A process according to claim 1, wherein said polyester is polyethylene terephthalate.
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) | 1987-07-31 | 1988-01-30 | 1988-07-31 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1991-07-31 | 1992-01-30 | 1992-07-31 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1995-07-31 | 1996-01-30 | 1996-07-31 | $7700.00 | Window Closed / Lapsed |