Patent US3715421A successfully refreshed from Google Patents.
US3715421A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the preparation of polyethylene terephthalate filaments
Assignee: Viscosuisse SA
•
Filing: 1970-04-15
•
Granted: 1973-02-06
•
Expires: 1990-04-15
Abstract
Abstract A continuous spin-draw process is disclosed for preparing highly drawn polyethylene terephthalate filaments drawn at speeds greater than 1,800 meters per minute using only one heated draw roll system without the use of any other heating device. Feed and draw rolls are provided with a surface roughness which allows a slipping of the filaments along a number of turns before they leave the feed rolls and after they arrive at the draw rolls. The filaments are partially drawn at the lower temperature of the feed rolls, drawing continues between the feed and draw rolls, and is completed at the higher temperature of the draw rolls with a total draw ratio between 5 and 8.
Inventors
- 👤 H Martin
- 👤 B Glutz
- 👤 H Linz
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-23 17:53
CPC Classifications
D; D02; D02J; D02J1/00; D02J1/22; D01; D01D; D01D5/00; D01D5/12; D01D5/16; D02J1/224; D02J1/225; D02J1/226; D01F; D01F6/00; D01F6/58; D01F6/62
Claims Analysis
Total Claims: 14
Claim 1
Independent Claim
302 words
Continuous process for the preparation of highly drawn polyethylene terephthalate filaments which comprises extruding molten polyethylene terephthalate through a spinnerette to form filaments, quenching the filaments, applying to the filaments a lubricating finish, passing the filaments successively over a feed roll system and a draw roll system, each system comprising at least two cylindrical rolls with each roll having a surface roughness with a roughness height as defined by ASA B 46.1 - 1962 of 0.5-2.2 microns, allowing a slipping of the filaments around the feed roll system and the draw roll system of one to five turns, driving at least one feed roll and one draw roll by a motor, arranging said systems so that the axis of the feed roll from which the filaments leave the feed roll system and the axis of the draw roll at which the filaments arrive at the draw roll system are parallel while the axes of at least two of the feed rolls of the feed roll system are skew set to each other and the axes of at least two of the draw rolls of the draw roll system are skew set to each other, gradually drawing the filaments, starting the drawing while the filaments pass around the last one to five turns before leaving the feed rolls which have a surface temperature of 75* - 130* C., and completing the drawing while the filaments pass around the first one to five turns after arrival on the draw rolls which have a surface temperature of 180* - 240* C. and a surface speed at least five times that of the feed rolls, drawing the filaments at a total draw ratio Of not less than 5.0, and finally winding up the drawn filaments at a speed of not less than 1,800 meters per minute.
Claim 2
Dependent Claim
302 words
Continuous process for the preparation of highly drawn polyethylene terephthalate filaments which comprises extruding molten polyethylene terephthalate through a spinnerette to form filaments, quenching the filaments, applying to the filaments a lubricating finish, passing the filaments successively over a feed roll system and a draw roll system, each system comprising at least two cylindrical rolls with each roll having a surface roughness with a roughness height as defined by ASA B 46.1 - 1962 of 0.5-2.2 microns, allowing a slipping of the filaments around the feed roll system and the draw roll system of one to five turns, driving at least one feed roll and one draw roll by a motor, arranging said systems so that the axis of the feed roll from which the filaments leave the feed roll system and the axis of the draw roll at which the filaments arrive at the draw roll system are parallel while the axes of at least two of the feed rolls of the feed roll system are skew set to each other and the axes of at least two of the draw rolls of the draw roll system are skew set to each other, gradually drawing the filaments, starting the drawing while the filaments pass around the last one to five turns before leaving the feed rolls which have a surface temperature of 75* - 130* C., and completing the drawing while the filaments pass around the first one to five turns after arrival on the draw rolls which have a surface temperature of 180* - 240* C. and a surface speed at least five times that of the feed rolls, drawing the filaments at a total draw ratio Of not less than 5.0, and finally winding up the drawn filaments at a speed of not less than 1,800 meters per minute.
Claim 3
Dependent Claim
23 words
Process as set forth in claim 1 including using a lubricating finish which contains not more than 10 percent by weight of water.
Claim 4
Dependent Claim
59 words
Process as set forth in claim 1, wherein the spun filaments before arriving at the feed roll system, pass over a pre-tension roll system comprising at least one unheated motor-driven roll, using a surface speed of the pre-tension unheated roll which is lower than the surface speed of the feed rolls with the speed difference not exceeding 2 percent.
Claim 5
Dependent Claim
55 words
Process as set forth in claim 1 including providing said rolls with a surface roughness range, as defined by DIN 4762, of 4.5 - 8.0 microns, a peak distance of not more than 140 microns, an average peak distance of 40 - 60 microns, and a profile curvature of not more than 0.030 microns 1.
Claim 6
Dependent Claim
21 words
Process as set forth in claim 4 including providing said rolls with an average roughness range of 1.6 - 3.0 microns.
Claim 7
Dependent Claim
21 words
Process as set forth in claim 1 including providing said rolls with a peak distance of not more than 140 microns.
Claim 8
Dependent Claim
20 words
Process in accordance with claim 6 including providing said rolls with an average peak distance of 40 - 60 microns.
Claim 9
Dependent Claim
21 words
Process in accordance with claim 1 including providing said rolls with a profile curvature of not more than 0.030 microns 1.
Claim 10
Dependent Claim
175 words
Continuous process for the preparation of highly-drawn polyethylene terephthalate filaments which comprises extruding molten polyethylene terephthalate through a spinnerette to form filaments, quenching the filaments, applying to the filaments a lubricating finish, passing the filaments over feed rolls and draw rolls which have a surface roughness which allows slipping of from one to five turns before the filaments leave the feed rolls and after the filaments arrive at the draw rolls, the feed rolls having a surface temperature of 75* - 130* C, and the draw rolls having a surface temperature of 180* - 240* C and a surface speed at least five times that of the feed rolls, partially drawing the filaments at the lower temperature of the feed rolls, continuing to draw the filaments between the feed rolls and the draw rolls, and completing the drawing of the filaments at the higher temperature of the draw rolls to attain a total draw ratio of 5 to 8, and winding up the drawn filaments at a speed of 1,800 to 6,000 meters per minute.
Claim 11
Dependent Claim
175 words
Continuous process for the preparation of highly-drawn polyethylene terephthalate filaments which comprises extruding molten polyethylene terephthalate through a spinnerette to form filaments, quenching the filaments, applying to the filaments a lubricating finish, passing the filaments over feed rolls and draw rolls which have a surface roughness which allows slipping of from one to five turns before the filaments leave the feed rolls and after the filaments arrive at the draw rolls, the feed rolls having a surface temperature of 75* - 130* C, and the draw rolls having a surface temperature of 180* - 240* C and a surface speed at least five times that of the feed rolls, partially drawing the filaments at the lower temperature of the feed rolls, continuing to draw the filaments between the feed rolls and the draw rolls, and completing the drawing of the filaments at the higher temperature of the draw rolls to attain a total draw ratio of 5 to 8, and winding up the drawn filaments at a speed of 1,800 to 6,000 meters per minute.
Claim 12
Dependent Claim
32 words
A process as set forth in claim 9 wherein the temperature of the feed rolls is 80* - 90* C, and the temperature of the draw rolls is 210* - 230* C.
Claim 13
Dependent Claim
23 words
Process as set forth in claim 9 including using a lubricating finish which contains not more than 10 percent by weight of water.
Claim 14
Dependent Claim
39 words
A process as set forth in claim 9 wherein said surface roughness consists of a coherent, non-porous, abrasion-resistant, impermeable coating of tiny, smooth-topped elevations of unequal height and irregular distribution in all directions on the surface of said rolls.
References Cited (Backward Citations)
CA611444A
Cited
CA628863A
Cited
US2851732A
Cited
US2859472A
Cited
US3009231A
Cited
US2990603A
Cited
US3101990A
Cited
GB1006348A
Cited
US3091805A
Cited
US3123891A
Cited
US3164650A
Cited
US3329758A
Cited
GB1011645A
Cited
US3400194A
Cited
US3422491A
Cited
US3485913A
Cited
US3433008A
Cited
GB1176164A
Cited
US3495295A
Cited
US3366721A
Cited
US3481136A
Cited
US3500519A
Cited
US3561045A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1976-02-06 | 1976-08-07 | 1977-02-06 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1980-02-06 | 1980-08-07 | 1981-02-06 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1984-02-06 | 1984-08-07 | 1985-02-06 | $7700.00 | Window Closed / Lapsed |