US2307846A - Production of synthetic structures - Google Patents
Production of synthetic structures Download PDFInfo
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- US2307846A US2307846A US272136A US27213639A US2307846A US 2307846 A US2307846 A US 2307846A US 272136 A US272136 A US 272136A US 27213639 A US27213639 A US 27213639A US 2307846 A US2307846 A US 2307846A
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- filaments
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
- D06M11/00—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising
- D06M11/01—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with hydrogen, water or heavy water; with hydrides of metals or complexes thereof; with boranes, diboranes, silanes, disilanes, phosphines, diphosphines, stibines, distibines, arsines, or diarsines or complexes thereof
- D06M11/05—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with inorganic substances or complexes thereof; Such treatment combined with mechanical treatment, e.g. mercerising with hydrogen, water or heavy water; with hydrides of metals or complexes thereof; with boranes, diboranes, silanes, disilanes, phosphines, diphosphines, stibines, distibines, arsines, or diarsines or complexes thereof with water, e.g. steam; with heavy water
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06M—TREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
- D06M13/00—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment
- D06M13/10—Treating fibres, threads, yarns, fabrics or fibrous goods made from such materials, with non-macromolecular organic compounds; Such treatment combined with mechanical treatment with compounds containing oxygen
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S264/00—Plastic and nonmetallic article shaping or treating: processes
- Y10S264/61—Processes of molding polyamide
Definitions
- This invention relates to synthetic linear polymers, and particularly to a process for improving the properties of shaped articles prepared from fiber-forming synthetic linear polyamides.
- This invention is concerned in particular with the new class of filament-forming materials known as synthetic linear polymers described in U. S. Patents Nos. 2,071,250; 2,071,251; 2,071,252 and 2,071,253.
- a characteristic property of these polymers is their crystallinity and the fact that filaments and the like prepared from them can be cold drawn, whereupon they show molecular orientation along the fiber axis.
- the cold drawn filaments are stronger and more elastic than the undrawn' filaments and are therefore more useful in the preparation of yarns and fabrics.
- Other articles prepared from these polymers e. g., bristles, ribbons, sheets, and rods, are likewise improved by cold drawing, cold rolling or other processes which bring about molecular orientation of the molecules.
- a particularly useful subclass of filamentforming linear polymers is that of the polyamides. These are of two types: those obtainable from polymerizable monoaminomonocarboxylic acids and their amide-forming derivatives, including caprolactam, and those obtainable from the reaction of suitable diamines with suitable dibasic carboxylic acids or their amideforming derivatives. The latter type is more fully described in U. S. Patent No. 2,130,948. In these polyamides theamide groups form an integral part of the main chain of atoms. The present invention will be described with particular reference to the polyamides, although it is to be understood that it is not so limited.
- Textile yarns may be shrunk (residual shrinkage removed) by a treatment of the yarns in the relaxed condition with hot water.
- Such treatments are usually accomplished by subjecting the yarn in skeins to the action of hot water whereupon the yarn decreases in length with anaccompanying decrease in residual shrinkageand increase in denier.
- This decrease in length of a textile yarn upon being subjected to a shrinkage treatment will be referred to as process shrinkage.
- This skein process is expensive as it must necessarily be discontinuous; likewise, the necessary v handling tends to degrade the yarn.
- Such a process is particularly objectionable in the case 'of polyamide yarns since they are spun directly from melt at very high spinning speeds making possible efficientand rapid continuous production.
- Another disadvantage in such a process is the decrease in length and increase in denier after shrinkage. This decrease in length and increase in denier may be non-uniform and is not easily controlled.
- the residual shrinkage of such structures is materially reduced, if not substantially eliminated, without subjecting them to process shrinkage.
- a polyamide structure can actually be stretched to a material extent, for example, or more, and set in such a stretched condition with a substantial reduction in residual shrinkage.
- residual shrinkage By the term residual shrinkage "is meant the percentage decrease in length which the filament or yarn undergoes when it is subjected in a relaxed condition to a hot aqueous treatment with or without detergents at temperatures of 95-100 C. for five minutes.
- determining residual shrinkage a measured sample is subjected to the shrinkage treatment described above and dried in a relaxed condition, whereupon its length is determined at the same humidity and tempera ture as the initial measurements and the percentage shrinkage calculated.
- a further object of this invention is the reduction of the residual shrinkage of oriented polyamide filaments, yarns and the like while they are maintained in such a manner that theycannot freely change their linear dimensions.
- Another object of this invention is the provision of a continuous method for removing the residual shrinkage of oriented polyamide filaments without accompanying shrinkage.
- the objects of this invention are accomplished, in general, by setting structures comprising oriented synthetic linear polyamide filaments, yarns, ribbons, sheets or the like by a treatment at elevated temperatures with hydroxylated or non-hydroxylated, non-solvent swelling agents for the polyamide while restraining the filaments, yarns, ribbons, sheetsor the like from any substantial reduction in linear dimensions, and in the case of ribbons and sheets, planar dimensions.
- a treatment at elevated temperatures with hydroxylated or non-hydroxylated, non-solvent swelling agents for the polyamide while restraining the filaments, yarns, ribbons, sheetsor the like from any substantial reduction in linear dimensions, and in the case of ribbons and sheets, planar dimensions.
- Example I A 45-denier, -filament polyhexamethylene adipamide yarn, cold drawn 410% with a Z twist of turns per inch, was wound under a tension of 10 grams, on an aluminum bobbin having a four-inch diameter. The bobbin was then placed in a steam chamber, subjected to saturated steam at 120 C. for 20 minutes and the yarnthen removed from the bobbin. This steamtreatment of the wound yarn set the yarn without noticeably shrinking the same. The residual shrinkage of the treated yarn was determined and found to be 1% as compared with a residual shrinkage of the untreated yarn of 7%.
- Example II A 45-denier, 15-filament polyhexamethylene adipamide yarn, drawn 376% having a twist of 4.5 turns per inch, was wound on a bobbin in the same manner as described in Example I, and was set by submerging the same in boiling water for five minutes. The residual shrinkage of the resultant yarn was 4% as compared with a residual shrinkage of the untreated yarn of 10.2%.
- Example III A woven fabric was constructed using 140 threads per inch of -denier, 10-filament, 10-
- the properties of the treated monofil were determined and found to be: denier, 13,800; tenacity (grams perdenier) 3.7; tensile strength (pounds to break) elongation (to break) 20%.
- the residual shrinkage was less than 0.5%.
- the invention may be practiced continuously by subjecting the yarn to hot-wet treatments while running continuously between rolls running at the same peripheral speed and gripping the yarn so that it cannot shrink. Such treatments may also be applied to ribbons, sheets, and woven fabrics in the same manner. Proper provisions may be made to prevent lateral shrinkage as by gripping belts, etc.
- the yarn can be treated withhot water or steam either at atmospheric or superatmospheric pressures.
- the yarn or fabric may travel will depend on the length of the length of the chamber in which the treatment is applied, the temperature of the setting agents and the reduction in residual shrinkage desired. The higher the temperature of the treatment and the longer the travel of the yarn, the higher the speed of travel permissible to maintain the same reduction in residual shrinkage.
- Organic non-solvent swelling agents for the polyamides are also useful. These may be hydroxylated compounds such as the aliphatic alcohols. Methanol, isopropanol and isobutanol are particularly'useful. Other hydroxyl-containing compounds which are useful include ethyl lactate, dimethyl tartrate, ethyl glycolate, ethanolamine, diacetone alcohol and polyhydric alcohols; e. g., ethylene glycol and glycerol. Useful compounds which do not contain the hydroxyl group include organic amines such as aniline, toluidine, dibutyl amine, etc., as well as nitriles and amides.
- the hydroxylated compounds such as the aliphatic alcohols. Methanol, isopropanol and isobutanol are particularly'useful.
- Other hydroxyl-containing compounds which are useful include ethyl lactate, dimethyl tartrate, ethyl glycolate, ethanolamine, diacetone alcohol and
- agents used according to this invention are that they have a swelling action on the polyamides without dissolving them; that is, they are substantially chemically inert towards polyamides.
- This requirement for a non-solvent, organic swelling agent may be satisfied by a mixture of a solvent and a non-solvent.
- any hot-wet treatment has a setting action on oriented polyamide articles, it is generally preferred to employ temperatures between 65 C. and 175 C. for periods of a few minutes to an hour.
- the setting treatment should be carried out at such a temperature and for such a period of time as to reduce the residual shrinkage of the polyamide structures at least to 75% of that of the unset structure.
- the temperature and period of treatment depend upon the particular polyamide and its physical form and upon the setting agent employed. Generally, the higher the temperature employed the shorter the period that is necessary.
- the degree of setting in a given time is roughly a linear function of temperature. For example, the preferred temperature range for water and saturated steam is 95 C. to 110 C. for times ranging from one to fifteen minutes. A treatment for one minute with saturated steam is approximately equivalent to a five minute treatment with hot water at 95 C. Similarly, a five minute treatment with methanol vapor at 100 C. produces as much setting as thirty minutes liquid treatment at 65 C.
- Dry heat is ineffective as an agent to substantially reduce residual shrinkage where the polyamide structure is held against shrinkage in accordance with the present invention.
- the process of this invention may also be practiced to advantage on articles made from other synthetic linear polymers such as the polyesters.
- the setting of polyamide structures in accordance with the present invention can be definitely discerned in the set structures.
- the setting treatment changes the crystalline characteristics of synthetic linear polyamide structures as evidenced by X-ray investigation.
- the X-ray diffraction patterns which change markedly upon cold drawing become much sharper after the yarn is subjected to the setting treatments of this invention. By X-ray investigation it can therefore be definitely ascertained whether or not a structure has been subjected to the process ofthis invention.
- the step which comprises setting said structures by treating the same with a non-solvent swelling agent for the polyamide at a temperature of between C. and 175 C. for a sumcient period of time to reduce the residual shrinkage of the structure at least to of that of a similar unset structure while preventing substantial reduction in dimension of said structures.
- step 2 which comprises setting said structure by treating the same with a non-solvent swelling agent for the polyamide at a temperature of between 65 C. and C. for a period of l to 15 minutes while preventing substantial reduction in dimension of said structures.
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- Engineering & Computer Science (AREA)
- Textile Engineering (AREA)
- Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
- Artificial Filaments (AREA)
Description
Patented Jan. 12, 1943 PRODUCTION OF SYNTHETIC STRUCTURES John B. Miles, Greenville, Dcl., assignor to E. I. du Pont dc Nemours & Company, Wilmington, Del., a corporation of Delaware No Drawing. Application May 6, 1939, Serial No. 272,136
, 12 Claims. This invention relates to synthetic linear polymers, and particularly to a process for improving the properties of shaped articles prepared from fiber-forming synthetic linear polyamides.
This invention is concerned in particular with the new class of filament-forming materials known as synthetic linear polymers described in U. S. Patents Nos. 2,071,250; 2,071,251; 2,071,252 and 2,071,253. A indicated in these patents, a characteristic property of these polymers is their crystallinity and the fact that filaments and the like prepared from them can be cold drawn, whereupon they show molecular orientation along the fiber axis. The cold drawn filaments are stronger and more elastic than the undrawn' filaments and are therefore more useful in the preparation of yarns and fabrics. Other articles prepared from these polymers; e. g., bristles, ribbons, sheets, and rods, are likewise improved by cold drawing, cold rolling or other processes which bring about molecular orientation of the molecules.
A particularly useful subclass of filamentforming linear polymers is that of the polyamides. These are of two types: those obtainable from polymerizable monoaminomonocarboxylic acids and their amide-forming derivatives, including caprolactam, and those obtainable from the reaction of suitable diamines with suitable dibasic carboxylic acids or their amideforming derivatives. The latter type is more fully described in U. S. Patent No. 2,130,948. In these polyamides theamide groups form an integral part of the main chain of atoms. The present invention will be described with particular reference to the polyamides, although it is to be understood that it is not so limited.
In my applications, Serial Nos. 125,941 and 227,014 filed February 15, 1937 and August 26, 1938, respectively, and in application Serial No. 183,922 filed by V. R. Hardy and myself January 7, 1938, there is disclosed the unusual setting effect of steam and hot water, and of hot liquids or vapors of organic non-solvent swelling agents for the polyamide or polyamide articles, that is, permanently setting the articles in a specially imposed form or shape to which they tend to recover after deformation.
- Such setting of articles comprising synthetic linear polymers, even when held under a slight tension, results in shrinkage.
Textile yarns (including oriented polyamide yarns) may be shrunk (residual shrinkage removed) by a treatment of the yarns in the relaxed condition with hot water. Such treatments are usually accomplished by subjecting the yarn in skeins to the action of hot water whereupon the yarn decreases in length with anaccompanying decrease in residual shrinkageand increase in denier. This decrease in length of a textile yarn upon being subjected to a shrinkage treatment will be referred to as process shrinkage. This skein process is expensive as it must necessarily be discontinuous; likewise, the necessary v handling tends to degrade the yarn. Such a process is particularly objectionable in the case 'of polyamide yarns since they are spun directly from melt at very high spinning speeds making possible efficientand rapid continuous production. Another disadvantage in such a process is the decrease in length and increase in denier after shrinkage. This decrease in length and increase in denier may be non-uniform and is not easily controlled.
It is known to stretch textile filaments such as cellulosic rayon and to subject them while in a stretched condition to the action of hot water followed by drying, whereupon the dried yarn is obtained in substantially the same dimensions- Such a condition, is, however, unstable, for upon being subsequently subjected to shrinking conditions the yarn shrinks and shows no permanent eifect of this intervening treatment under tension. In fact, such processes are used to produce yarns of abnormally high shrinkage for special purposes.
It ha now been found that oriented synthetic linear polyamide filaments, sheets, and ribbons, as well as synthetic linear polyamide articles such as yarns and woven fabrics constructed from such oriented filaments, and in which construction the linear dimensions of the filaments can be restrained from shrinkage (in knitted goods, for example, the linear dimensions of the filaments cannot be restrained from shrinkage), can I be set in their preshrunk dimensions by subjecting them to setting conditions while restraining the filaments, ribbons or yarns from any reduction in linear dimensions, and in the case of ribbong and sheets, planar dimensions. These structures, when so treated, tend always to retain their set dimensions even though they are subsequently exposed in a relaxed state to conditions which would result in shrinkage of previously unset structures. That is to say, the residual shrinkage of such structures is materially reduced, if not substantially eliminated, without subjecting them to process shrinkage. Althougn of less importance, it has been found that a polyamide structure can actually be stretched to a material extent, for example, or more, and set in such a stretched condition with a substantial reduction in residual shrinkage.
By the term residual shrinkage"'is meant the percentage decrease in length which the filament or yarn undergoes when it is subjected in a relaxed condition to a hot aqueous treatment with or without detergents at temperatures of 95-100 C. for five minutes. In determining residual shrinkage a measured sample is subjected to the shrinkage treatment described above and dried in a relaxed condition, whereupon its length is determined at the same humidity and tempera ture as the initial measurements and the percentage shrinkage calculated.
It is therefore an object of this invention to set structures comprising oriented synthetic linear polyamide filaments, yarns, ribbons, sheets or the like while restrainingthe filaments, yarns, ribbons, sheets or the like from' any substantial reduction in linear dimensions, and in the case of ribbons and sheets, planar dimensions.
It is a further object of this invention'to provide a, process for reducing the residual shrinkage of oriented polyamide articles without allowing them to shrink.
A further object of this invention is the reduction of the residual shrinkage of oriented polyamide filaments, yarns and the like while they are maintained in such a manner that theycannot freely change their linear dimensions.
Another object of this invention is the provision of a continuous method for removing the residual shrinkage of oriented polyamide filaments without accompanying shrinkage.
Other objects of this invention will hereinafter become apparent.
The objects of this invention are accomplished, in general, by setting structures comprising oriented synthetic linear polyamide filaments, yarns, ribbons, sheets or the like by a treatment at elevated temperatures with hydroxylated or non-hydroxylated, non-solvent swelling agents for the polyamide while restraining the filaments, yarns, ribbons, sheetsor the like from any substantial reduction in linear dimensions, and in the case of ribbons and sheets, planar dimensions. The following specific examples are illustrative of the details of the invention. It is to be understood that the invention is not limited to the details set forth therein.
Example I A 45-denier, -filament polyhexamethylene adipamide yarn, cold drawn 410% with a Z twist of turns per inch, was wound under a tension of 10 grams, on an aluminum bobbin having a four-inch diameter. The bobbin was then placed in a steam chamber, subjected to saturated steam at 120 C. for 20 minutes and the yarnthen removed from the bobbin. This steamtreatment of the wound yarn set the yarn without noticeably shrinking the same. The residual shrinkage of the treated yarn was determined and found to be 1% as compared with a residual shrinkage of the untreated yarn of 7%.
Example II A 45-denier, 15-filament polyhexamethylene adipamide yarn, drawn 376% having a twist of 4.5 turns per inch, was wound on a bobbin in the same manner as described in Example I, and was set by submerging the same in boiling water for five minutes. The residual shrinkage of the resultant yarn was 4% as compared with a residual shrinkage of the untreated yarn of 10.2%.
Example III A woven fabric was constructed using 140 threads per inch of -denier, 10-filament, 10-
turn 8 twist dull yarn of oriented polyhexamethylene adipamide as the warp, and 120 threads per inch of 35-denier, 10-filament, 10-turn S twist dull yarn of oriented polyhexamethylene adipamide in the filling. A portion of this fabric was tightly stretched on'a tentering frame and held against substantial shrinkage while subjecting the same to the action of saturated steam at C. for 15 minutes. A sample of this fabric when subjected to the conditions used in determining residual shrinkage of a yarn and measured in the warp and filling direction will be found to shrink approximately 1%. A sample of a similar untreated fabric when tested in the same manner will be found to shrink approximately 5%.
Example IV strain against reduction in linear dimension and placed in an autoclave and subjected to saturated steam at a pressure of '70 pounds per square inch for 30 minutes. The properties of the treated monofil were determined and found to be: denier, 13,800; tenacity (grams perdenier) 3.7; tensile strength (pounds to break) elongation (to break) 20%. The residual shrinkage was less than 0.5%.
The invention may be practiced continuously by subjecting the yarn to hot-wet treatments while running continuously between rolls running at the same peripheral speed and gripping the yarn so that it cannot shrink. Such treatments may also be applied to ribbons, sheets, and woven fabrics in the same manner. Proper provisions may be made to prevent lateral shrinkage as by gripping belts, etc. The yarn can be treated withhot water or steam either at atmospheric or superatmospheric pressures. the yarn or fabric may travel will depend on the length of the length of the chamber in which the treatment is applied, the temperature of the setting agents and the reduction in residual shrinkage desired. The higher the temperature of the treatment and the longer the travel of the yarn, the higher the speed of travel permissible to maintain the same reduction in residual shrinkage.
While in the foregoing examples this invention has been illustrated by hot-wet treatments involving hot water or steam it is not so limited. Organic non-solvent swelling agents for the polyamides are also useful. These may be hydroxylated compounds such as the aliphatic alcohols. Methanol, isopropanol and isobutanol are particularly'useful. Other hydroxyl-containing compounds which are useful include ethyl lactate, dimethyl tartrate, ethyl glycolate, ethanolamine, diacetone alcohol and polyhydric alcohols; e. g., ethylene glycol and glycerol. Useful compounds which do not contain the hydroxyl group include organic amines such as aniline, toluidine, dibutyl amine, etc., as well as nitriles and amides. The
The speed at which use of dilute aqueous solutions of alkali metal sulfltes; e. g. sodium sulfite, is particularly effective. The only requirement of agents used according to this invention is that they have a swelling action on the polyamides without dissolving them; that is, they are substantially chemically inert towards polyamides. This requirement for a non-solvent, organic swelling agent may be satisfied by a mixture of a solvent and a non-solvent. Setting agents which are effective produce at least 1% increase in the length of the unoriented filament at 25 C. and preferably They should also be tested at the setting temperature to be sure they are not active solvents.
While any hot-wet treatment has a setting action on oriented polyamide articles, it is generally preferred to employ temperatures between 65 C. and 175 C. for periods of a few minutes to an hour. In order to obtain the advantages of the present invention the setting treatment should be carried out at such a temperature and for such a period of time as to reduce the residual shrinkage of the polyamide structures at least to 75% of that of the unset structure. The temperature and period of treatment depend upon the particular polyamide and its physical form and upon the setting agent employed. Generally, the higher the temperature employed the shorter the period that is necessary. The degree of setting in a given time is roughly a linear function of temperature. For example, the preferred temperature range for water and saturated steam is 95 C. to 110 C. for times ranging from one to fifteen minutes. A treatment for one minute with saturated steam is approximately equivalent to a five minute treatment with hot water at 95 C. Similarly, a five minute treatment with methanol vapor at 100 C. produces as much setting as thirty minutes liquid treatment at 65 C.
Dry heat is ineffective as an agent to substantially reduce residual shrinkage where the polyamide structure is held against shrinkage in accordance with the present invention.
. While this invention has been described with particular emphasis on yarns consisting solely of oriented linear polyamide filaments, it is also applicable to mixed textile materials. Similarly, yarns comprising staple length polyamide filaments alone or in combination with other textile Likewise, mixed fabrics may be treated according to this invention. This invention is also appliable to oriented polyamide filaments, yarns and the like comprising modifying agents, for eX- ample, luster-modifying agents, delusterants, etc.
The process of this invention may also be practiced to advantage on articles made from other synthetic linear polymers such as the polyesters.
etc., described in U. S. Patent No. 2,071,251, as
well as articles made from polyester-amide interpolymers.
The setting of polyamide structures in accordance with the present invention can be definitely discerned in the set structures. The setting treatment changes the crystalline characteristics of synthetic linear polyamide structures as evidenced by X-ray investigation. The X-ray diffraction patterns which change markedly upon cold drawing become much sharper after the yarn is subjected to the setting treatments of this invention. By X-ray investigation it can therefore be definitely ascertained whether or not a structure has been subjected to the process ofthis invention.
By the practice of this invention it is possible to produce, continuously or discontinuously, oriented polyamide filaments, yarns, and the like having a uniformly low residual shrinkage by I treatment whereby the linear dimensions or the yarn are not materially reduced. It is therefore possible to produce woven fabrics and the like which will not shrink appreciably upon subsequent treatment with hot water, steam or other non-solvent swelling agents for the. polyamides and in which the structure of the fabric is not injured by shrinking treatment. Yarns treated in accordance with this invention can also be used for the production of knitted fabrics which will not shrink appreciably in hot water, steam, and the like. Furthermore, the same treatments which are used to remove the residual shrinkage when applied to fabrics impart to them substantially permanent crease resistance. Since it is possible to reduce the residual shrinkage without undergoing shrinkage, there is no loss of length so that the yarns produced can be used more efliciently and effectively than those produced by other processes.
Since it is obvious that many changes and modifications can be made in the details of the invention above set forth, it is to be understood that the invention is not to be limited except as set forth in the appended claims.
I claim:
1. In a process for reducing the residual shrinkage of oriented synthetic linear polyamide structures of filaments, yarns, ribbons, sheets and woven fabrics the construction of which will permit prevention ofshrinkage of filaments and yarns 'of which they are made, the step which comprises setting said structures by treating the same with a non-solvent swelling agent for the polyamide at a temperature of between C. and 175 C. for a sumcient period of time to reduce the residual shrinkage of the structure at least to of that of a similar unset structure while preventing substantial reduction in dimension of said structures.
2. In a process for reducing the residua. shrinkage of oriented synthetic linear polyamide structures of filaments, yarns, ribbons, sheets and woven fabrics the construction of which will permit prevention of shrinkage of filaments and yarns of which they are made, the step which comprises setting said structure by treating the same with a non-solvent swelling agent for the polyamide at a temperature of between 65 C. and C. for a period of l to 15 minutes while preventing substantial reduction in dimension of said structures.
3. In a process for reducing the residual shrinkage of woven fabric the construction of which will permit prevention of shrinkage of filaments and yarns of which it is made and in which said filaments and yarns are composed of oriented synthetic linear polyamides which comprises subjecting said yams and filaments to a setting treatment with a non-solvent swelling agent for the polyamide at a temperature of 65 C. to 175 C. for a period of 1 to 15 minutes while preventing substantial reduction in linear dimension of said filaments and yarns.
4. In a process for reducing the residual shrinkage of filaments and yarns composed of oriented synthetic linear polyamides which comprises setting said filaments and yarns by treating the same with a non-solvent swelling agent for the polyamide at a temperature of 65 C. to 175 C. for a period of 1 to 15 minutes while preventing substantial reduction in linear dimension oiv said filaments and yarns.
5. In a process for reducing the residual shrinkage of filaments and yarns composed of oriented synthetic linear polyamides which comprises continuously setting said filaments and yarns by treating the same with a non-solvent swelling agent for the polyamide at a temperature of 65 C. to 175 C. for a period 01 1 to 15 minutes while preventing substantial reduction in linear dimension of said filaments and yarns.
6. In a process for reducing the residual shrinkage of sheets and ribbons composed of oriented synthetic linear polyamides which comprises setting said sheets and ribbons by. treating the same with a non-solvent swelling agent for the polyamide at a temperature 01' 65 C to JOHN B. MILES.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
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BE464210D BE464210A (en) | 1939-05-06 | ||
US272136A US2307846A (en) | 1939-05-06 | 1939-05-06 | Production of synthetic structures |
FR926624D FR926624A (en) | 1939-05-06 | 1946-03-19 | Process for obtaining articles made of synthetic products |
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US272136A US2307846A (en) | 1939-05-06 | 1939-05-06 | Production of synthetic structures |
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US272136A Expired - Lifetime US2307846A (en) | 1939-05-06 | 1939-05-06 | Production of synthetic structures |
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Cited By (23)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2484523A (en) * | 1945-01-04 | 1949-10-11 | Du Pont | Process for making polyamide filaments |
US2509741A (en) * | 1942-11-03 | 1950-05-30 | Du Pont | Production of filamentous structures |
US2537666A (en) * | 1945-08-10 | 1951-01-09 | Dow Chemical Co | Producing thick sheets from thin films |
US2541839A (en) * | 1949-07-22 | 1951-02-13 | Du Pont | Process for improving vat dyed nylon fibers |
US2554564A (en) * | 1947-06-24 | 1951-05-29 | Celanese Corp | Prestretching cellulose derivative yarns to increase tenacity |
US2615784A (en) * | 1949-12-20 | 1952-10-28 | Du Pont | Polyethylene terephthalate monofils drawn and heat set for use as bristles |
US2652093A (en) * | 1949-03-02 | 1953-09-15 | Gates Rubber Co | Method of making reinforced rubber hose |
US2670267A (en) * | 1950-05-02 | 1954-02-23 | Du Pont | Heat-treatment of n-alkyl polyamides |
US2679088A (en) * | 1949-05-05 | 1954-05-25 | Goodyear Tire & Rubber | Method of treating thermoplastic web |
US2956330A (en) * | 1957-05-23 | 1960-10-18 | Du Pont | Stabilized yarn |
US2995178A (en) * | 1956-09-04 | 1961-08-08 | Us Rubber Co | Method of making pneumatic tires |
US3021570A (en) * | 1956-09-19 | 1962-02-20 | Podesta Armando | Process for the manufacture of hollow articles from thermoplastic resin blanks by cold extrusion |
US3024152A (en) * | 1957-11-04 | 1962-03-06 | Johnson & Johnson | Stabilized polymeric strand reinforced pressure sensitive adhesive tapes |
US3084393A (en) * | 1958-01-14 | 1963-04-09 | Bayer Ag | Process for stretching filaments |
US3088792A (en) * | 1959-06-29 | 1963-05-07 | American Enka Corp | Thermoplastic yarns |
US3088794A (en) * | 1960-08-26 | 1963-05-07 | Du Pont | Process for spinning and drawing polyalkylene isophthalamides |
US3116356A (en) * | 1958-01-31 | 1963-12-31 | Basf Ag | Methods of producing homogeneous polyamide printing plate supports |
US3118011A (en) * | 1962-07-03 | 1964-01-14 | Du Pont | Process for preparing helically crimped composite filaments |
US3133138A (en) * | 1958-12-19 | 1964-05-12 | Du Pont | Stretching and heat crystallization of poly(meta-phenylene isophthalamide) fibers |
US3223526A (en) * | 1959-05-28 | 1965-12-14 | Minnesota Mining & Mfg | Printing processes including size reduction of graphic intelligence |
DE1207547B (en) * | 1958-08-09 | 1965-12-23 | Rhodiaceta Ag | Process for improving the properties of polyhexamethylene adipamide threads |
DE1209239B (en) * | 1956-10-29 | 1966-01-20 | Trikotfabriken J Schiesser A G | Process for drawing a melt-spun hollow filament |
US3871819A (en) * | 1968-03-06 | 1975-03-18 | James E Greer | Continuous liquid treatment of textile materials |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE866035C (en) * | 1950-09-16 | 1953-02-05 | Wilhelm J H Hinrichs | Process for improving the properties of polycondensation synthetic resin threads and knitted and woven goods made from them |
-
0
- BE BE464210D patent/BE464210A/xx unknown
-
1939
- 1939-05-06 US US272136A patent/US2307846A/en not_active Expired - Lifetime
-
1946
- 1946-03-19 FR FR926624D patent/FR926624A/en not_active Expired
Cited By (23)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2509741A (en) * | 1942-11-03 | 1950-05-30 | Du Pont | Production of filamentous structures |
US2484523A (en) * | 1945-01-04 | 1949-10-11 | Du Pont | Process for making polyamide filaments |
US2537666A (en) * | 1945-08-10 | 1951-01-09 | Dow Chemical Co | Producing thick sheets from thin films |
US2554564A (en) * | 1947-06-24 | 1951-05-29 | Celanese Corp | Prestretching cellulose derivative yarns to increase tenacity |
US2652093A (en) * | 1949-03-02 | 1953-09-15 | Gates Rubber Co | Method of making reinforced rubber hose |
US2679088A (en) * | 1949-05-05 | 1954-05-25 | Goodyear Tire & Rubber | Method of treating thermoplastic web |
US2541839A (en) * | 1949-07-22 | 1951-02-13 | Du Pont | Process for improving vat dyed nylon fibers |
US2615784A (en) * | 1949-12-20 | 1952-10-28 | Du Pont | Polyethylene terephthalate monofils drawn and heat set for use as bristles |
US2670267A (en) * | 1950-05-02 | 1954-02-23 | Du Pont | Heat-treatment of n-alkyl polyamides |
US2995178A (en) * | 1956-09-04 | 1961-08-08 | Us Rubber Co | Method of making pneumatic tires |
US3021570A (en) * | 1956-09-19 | 1962-02-20 | Podesta Armando | Process for the manufacture of hollow articles from thermoplastic resin blanks by cold extrusion |
DE1209239B (en) * | 1956-10-29 | 1966-01-20 | Trikotfabriken J Schiesser A G | Process for drawing a melt-spun hollow filament |
US2956330A (en) * | 1957-05-23 | 1960-10-18 | Du Pont | Stabilized yarn |
US3024152A (en) * | 1957-11-04 | 1962-03-06 | Johnson & Johnson | Stabilized polymeric strand reinforced pressure sensitive adhesive tapes |
US3084393A (en) * | 1958-01-14 | 1963-04-09 | Bayer Ag | Process for stretching filaments |
US3116356A (en) * | 1958-01-31 | 1963-12-31 | Basf Ag | Methods of producing homogeneous polyamide printing plate supports |
DE1207547B (en) * | 1958-08-09 | 1965-12-23 | Rhodiaceta Ag | Process for improving the properties of polyhexamethylene adipamide threads |
US3133138A (en) * | 1958-12-19 | 1964-05-12 | Du Pont | Stretching and heat crystallization of poly(meta-phenylene isophthalamide) fibers |
US3223526A (en) * | 1959-05-28 | 1965-12-14 | Minnesota Mining & Mfg | Printing processes including size reduction of graphic intelligence |
US3088792A (en) * | 1959-06-29 | 1963-05-07 | American Enka Corp | Thermoplastic yarns |
US3088794A (en) * | 1960-08-26 | 1963-05-07 | Du Pont | Process for spinning and drawing polyalkylene isophthalamides |
US3118011A (en) * | 1962-07-03 | 1964-01-14 | Du Pont | Process for preparing helically crimped composite filaments |
US3871819A (en) * | 1968-03-06 | 1975-03-18 | James E Greer | Continuous liquid treatment of textile materials |
Also Published As
Publication number | Publication date |
---|---|
FR926624A (en) | 1947-10-07 |
BE464210A (en) |
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