US2777750A - Process of stabilizing thermoplastic knitted fabric containing cellulose ester yarns with superheated steam - Google Patents

Process of stabilizing thermoplastic knitted fabric containing cellulose ester yarns with superheated steam Download PDF

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US2777750A
US2777750A US320282A US32028252A US2777750A US 2777750 A US2777750 A US 2777750A US 320282 A US320282 A US 320282A US 32028252 A US32028252 A US 32028252A US 2777750 A US2777750 A US 2777750A
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fabric
yarns
superheated steam
treatment
cellulose ester
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US320282A
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Basil S Sprague
Murray N Carroll
Robert H Roughsedge
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Celanese Corp
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Celanese Corp
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    • DTEXTILES; PAPER
    • D06TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06MTREATMENT, NOT PROVIDED FOR ELSEWHERE IN CLASS D06, OF FIBRES, THREADS, YARNS, FABRICS, FEATHERS OR FIBROUS GOODS MADE FROM SUCH MATERIALS
    • D06M11/00Treating 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
    • D06M11/01Treating 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
    • D06M11/05Treating 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

Definitions

  • This invention relates to the treatment of textile fabrics and relates more particularly to a process and apparatus for the treatment of knitted fabrics containing yarns of cellulose acetate or other organic acid esters of cellulose.
  • a further object of this invention is the provision of a process and apparatus for the treatment of knitted fabrics containing yarns of cellulose acetate or other organic acid esters of cellulose which will impart to said fabrics a high degree of dimensional stability.
  • a knitted fabric containing yarns of cellulose acetate or other organic acid esters of cellulose carrying a film of liquid water is raised to an elevated temperature in a gaseous atmoswhile the fabric is held to phere, preferably of steam,
  • the fabric is supported througha definite width and while the out substantially its entire area.
  • the wet fabric is maintained at the elevated temperature until the cellulose acetate or other organic acid ester of cellulose of which the yarns are composed is swollen and any internal stresses in the yarns are released, but care should be taken so as not to cause the yarns or the fibers making up the yarns to fuse or coalesce one with the other.
  • the moisture content of the fabric should not fall below its saturation regain value, which is defined as the moisture regain value of the fabric in contact with an atmosphere of relative humidity at the temperature of the fabric.
  • the fabric is cooled and, if desired, dried. Following this treatment, it is found that the fabric exhibits a high degree of dimensional stability so that garments made of said fabric will, from a practical viewpoint, retain their shape and dimensions substantially unchanged during normal use.
  • a wet knitted fabric of cellulose acetate is subjected to superheated steam, and the moisture content of the fabric before contact with the superheated steam and the time of contact with the superheated steam are so regulated that the excess surface moisture on the fabric is not completely evaporated and the moisture content of the fabric does not fall below its saturation regain value. That is, despite the evaporation of some of the water due to the drying effect of the superheated steam, an excess of water is maintained on the surface of the yarns throughout the exposure to the superheated steam. Thepresence of this excess of water is critical. If the moisture content of the fabric is below the 100 C. saturation regain value when it is first placed into contact with the superheated steam, adequate dimensional stability will not be obtained. if, on the other hand, through evaporation the moisture content drops below the saturation regain value during contact with the superheated steam the yarns of cellulose acetate will deluster.
  • the fabric advantageously should have a water content prior to steam treatment of at least about 20% by weight, preferably at least 50% byweight, based on the weight of the dried fabric, to insure that the water content of all portions of the fabric is above the minimum value, thereby avoiding dry spots whose dimensional stability will differ from that of the remainder of the treated fabric.
  • the maximum water content of the fabric should normally not exceed about by weight to avoid the necessity of heating large quantities of water to an elevated temperature during the steam treatment. Moreover, it is difficult to distribute such larger quantities of water in a uniform manner throughout the fabric before the treatment with steam.
  • the presence of uniformly distributed larger quantities of water in the fabric will, however, not interfere with the successful treatment of the fabric to impart a high degree of dimensional stability thereto.
  • the desired amount of water may be added to a dry knitted fabric to prepare it for treatment in accordance with the process of this invention.
  • the process is best applied to the fabric immediately following the final liquid treatment constituting a step in the finishing of the fabric.
  • the fabric in its wet condition following a wet finishing treatment is first treated to reduce its water content to the desired level, as by centrifuging, and then stretched by about 5 to 30% to a definite width before being subjected to the heat treatment in the manner set forth above.
  • the knitted cellulose ester fabric while being stabilized may have thereon any of the softening and antistatic, finishes usually applied to such fabrics.
  • the wet fabric is treated, in accordance with this invention, with steam while it is held to a definite width and while it is supported throughout substantially its entire area.
  • One form of apparatus for carrying out this treatment comprises a chamber provided with an inlet and exit slot, through Which the fabric enters and leaves the chamber, and equipped with tenter chains for holding the fabric to a definite width and moving the fabric continuously through the chamber.
  • tenter chains for holding the fabric to a definite width and moving the fabric continuously through the chamber.
  • rollers other means such as screens, belts or the like may be used to support the fabric during the treatment.
  • the fabric moves through the chamber it is treated with steam which is advantageously introduced into the chamber through distributing heads positioned both above and below the fabric at a plurality of points spaced along the path of the fabric.
  • the steam raises the temperature of the fabric to a point where the wet cellulose acetate or other organic acid ester of cellulose comprising the yarns of the fabric is swollen and in a condition in which the internal stresses in the yarns are released rapidly. This temperature is preferably about 100 C.
  • the steam treatment should, however, not be continued to a point where the yarns or the fibers making up the yarn tend to coalesce or where the hand of the fabric in changed in an undesirable manner.
  • the fabric It is essential that the fabric be supported throughout its entire area while it is at this elevated temperature. If no such support is provided, the fabric will tend to sag and be distorted due to its weight, thereby introducing stresses which will be locked into the fabric during the treatment and will cause dimensional changes in the fabric during use.
  • the superheated steam which is desirably at atmospheric pressure and at a temperature above about 230 F.', preferably in the range of about 240 F. to 250 F., is admitted to the chamber through a plurality of openings.
  • the spacing of the openings throughout the chamber is such that there is obtained an even distribution of steam throughout the area of the chamber.
  • the entering steam is caused to impinge on the fabric at fairly high velocity so as to effect an efiicient transfer of heat to the fabric.
  • a very even-steam distribution is necessary because of the previously described hazard of delustering which occurs if the fabric is over dried at any point during passage through the stabilization chamber.
  • the waste steam is exhausted from the chamber by means of exhaust ducts mounted at the side of the chamber. 7
  • the exhaust rate is adjusted so that the rate of removal of spent steam at the exhaust ducts does not quite balance the input rate. That is, more steam is admitted to the chamber than is removed through the exhaust ducts.
  • these exit and inlet slots have mounted, above and below, slotted. conduits through which heated air is forced. These conduits are mounted and aligned so that the heated air from the slots forms an air curtain through which the fabric passes. This air curtain further serves to dilute the-escaping steam and prevent condensation on the surrounding equipment.
  • the wet fabric may be preheated in any desired manner to an elevated temperature below the stabilizing treatment temperature prior to its entry into the chamber so as to reduce the period of time needed for the steam to bring the fabric to the treatment temperature.
  • the time of treatment varies, depending upon alarge number of factors, including the percentage of water present initially in the fabric, the temperature at which the Wet fabric enters the chamber, the weight of the fabric, the steam temperature, the degree of suprheat and the like. Control of the time of treatment is effected by adjusting the rate at which the fabric passes through the chamber, that is, by regu lating the speed of the tenter chains.
  • the fabric is cooled. At least during the preliminary stages of the cooling, the fabric should be held to a definite width and supported throughout its entire area so as to avoid imposing stresses upon the hot fabric. Cooling may be eifected simply by passing the fabric through the air, or, if desired, the rate of cooling may be accelerated by passing a stream of cool air over the fabric.
  • any further drying of the fabric that may be necessary is carried out by passing the fabric through a dryer of any desired type. It is preferred to reduce the moisture content of the cellulose acetate to about 5 to 7% regain. Over-drying tends to impart an objectionably harsh hand to the fabric.
  • the dried fabric exhibits a high degree. of dimensional stability and is eminently suited for a Wide variety of applications.
  • FIG. 1 is a side view of the apparatus, partly in section
  • Fig. 2 is a cross-sectional view of the apparatus, taken on the line 2-2 in Fig. l, in the direction of the arrows
  • Fig. 3 is a cross-sectional view of the apparatus, taken on the line 3-3 in Fig. l, in the direction of the arrows
  • Fig. 4 is a detail view of the upper steam distributor
  • Fig. 5 is a detail view of the lower steam distributor.
  • the reference numeral 11 designates a fabric whose edges are secured to tender chains 12 that act to hold the fabric at a definite width.
  • the tenter chains 12 are mounted on supports, indicated generally by reference numeral 13, that may be operated by means of hand wheeis 14 to adjust the lateral spacing between the tenter chains 12 in'a manner Well known in the art.
  • the tenter chains 12 carry the fabric 11 between a pair of heaters 15 equipped with infra-red heating elements to effect a preheating of the said fabric.
  • the tenter chains 12 carry the fabric 11 between a pair of heaters 15 equipped with infra-red heating elements to effect a preheating of the said fabric.
  • the treating chamber 16 comprises a shell 17 that is supported on. a framework 18.
  • the top 19 and upper portion of the ends 21 of the shell 17 are of double wall construction and a heating fluid such as steam is passed through said walls to raise them to an elevated temperature so that no water will condense on said walls to drop onto the fabric 11.
  • a heating fluid such as steam is passed through said walls to raise them to an elevated temperature so that no water will condense on said walls to drop onto the fabric 11.
  • a plurality of rubbe covered rolls 22 Positioned in the chamber 16 are a plurality of rubbe covered rolls 22 that extend transversely of the chamber between the tenter chains 12 and act to support the fabric during its treatment.
  • the rolls 22 are driven at a peripheralspeed equal to the linear speed of the tenter chains 12 by means of a motor 23 through a variable speed drive 24, a chain 25 and a series ofchains 26 and sprockets 27 that act to interconnectall'said rolls.
  • Steam is introduced into the chamber 16 through a plurality of lower distributors, indicated generally by reference nu-. meral 28, that are positioned between the rolls 22 beneath the fabric 11, and a plurality of upper distributors, indicated generally by reference numeral 29, that :are positioned above the fabric 11. 7 i
  • each of the lower distributors 28 -compnses a conduit 31 supported on a pedestal 32 (Fig. and having, a slot 33 extending through the uppermostportion thereof for the discharge of the steam which is supplied to-said lower distributors from headers 34.
  • the upper distributors 29 each comprises an elongated rectangular enclosure 35 to which steam is supplied by headers 36 through conduits 37. Extending longitudinally of the enclosure 35 are partitions 38 having apertures 39 therein which act to distribute the steam emerging from the conduits 37 more uniformly.
  • a pair of conduits 41 extending the full length of the enclosure 35 and being spaced apart a short distance to provide a passageway 42 therebetween.
  • a heating fluid such as steam, which may be at a higher temperature than the steam in the headers 36, is introduced into the conduits .1 from a header 43 and is discharged from said conduits through a header 44. All the steam flowing through the passageway 42 will come into intimate contact with the heated surfaces of the conduits 41. thereby turning into steam any drops of water that may be present in the steam emerging from the headers 36.
  • conduits 45 and 45 having slots 46 and 46' therein that face toward the fabric 11. Heated air under pressure is introduced into the conduits 45 and 45' and flows through the slots 46 and 46' toward the fabric 11 thereby acting as an air curtain to prevent the flow of cold atmospheric air into the chamber 16 and also acting to assist in the preheating of the said fabric.
  • the chamber 16 is provided with exhaust ducts 47 through which pass a constant flow of steam together with any air that may enter into the chamber during operation.
  • the fabric 11 Upon leaving the chamber 16, the fabric 11 passes through a cooling section, indicated generally by reference numeral 48. in at least the first portion of the cooling section 48, the fabric 11 is held at a definite width and. supported throughout substantially its entire area in the same manner as during its passage through the chamber 16, namel by the tenter chains 12 and rolls 22. Cooling of the fabric 11 may be effected simply through the action of atmospheric air. However, if desired, means such as slotted conduits, fans or the like may be provided for producing a forced flow of a cooling medium, such as air, over the fabric 11 and, if even more rapid cooling is desired, the cooling medium may be refrigerated.
  • a cooling medium such as air
  • Means may be provided for supporting the fabric throughout its entire area as it passes through the dryer 49, although this has been found unnecessary when the drying conditions are not severe.
  • such supporting means is desirable to prevent the introduction of a small, but not highly objectionable, degree of dimensional instability into the fabric 11.
  • the lateral spacing between the tent-er chains 12 may be widened slightly, e. g. by about 4%, as these chains pass through the drier, in order to avoid any substantial sagging of the fabric in the drier.
  • Example- A large number ofpieces of fabric warp knittedof 55 denier yarns of cellulose acetate having an acetyl value of 54.5%, measured as combined acetic acid, are scoured, dyed and washed and are then centrifuged to bring their moisture content to about based on the dry weight of the fabric.
  • the wet fabrics which are at room ternperature and have a width of about 90 inches, are sewn end to end and are then passed one after another through the apparatus shown in the drawings, without using preheater 15, at the rate of about 1300 pounds of wet fabric per hour while the fabrics are maintained at a width of ill inches and while saturated steam at: a pressure of 150 pounds per square inch gauge is passed at therate of about 5,000 pounds per hour through a throttling valve (not shown), through which it expands in an essentially adiabatic manner into the conduits leading to the lower distributors 28, upper distributors 29 and conduits 41.
  • the overall temperature of the treating chamher is above 230 F. After a treatment time of 15 seconds, the fabric is cooled and dried.
  • the dried fabrics when laundered in an automatic washer at F. and dried in substantially tensionless condition, exhibit an average area shrinkage of less than 4%. Subsequent laundering efiects no appreciable change in dimensions. When similar pieces of the same fabric are finished and dried in conventional manner they exhibit an average area shrinkage of 15% to 30% after the first washing.
  • a process for improving the dimensional stability of knitted fabric containing a thermoplastic lower aliphatic acid ester of cellulose yarns which comprises subjecting said knitted fabric, wetted with at least 20% of water based on the weight of the dried fabric, to superheated steam having a temperature above about 233 F, maintaining said fabric at a definite width and at a moisture content above the saturation regain value of said cellulose ester throughout the treatment'with superheated steam, said treatment with superheated'steam being continued until said cellulose ester is swollen and the internal stresses in the yarns are released and the dimensions of the fabric are stabilized to subsequent washing, the time and temperature of said treatment being insuiicient to efiect fusion or coalescence of said yarns, removing the fabric from contact with the superheated steam before the moisture content of said cellulose ester has been reduced below said saturation regain value so that said fabric still carries an excess of water on the surface of said yarns, and cooling the treated fabric, said fabric being supported throughout substantially its entire area while
  • a process for improving the dimensional stability of knitted fabric containing cellulose acetate yarns which comprises subjecting said knitted fabric, wetted with at least 20% of Water based onthe weight of the dried fabric, to superheated steam having a temperature above about 230 F., maintaining said fabric at adefinite width and at a moisture content above the saturation regain value of said cellulose ester throughout the treatment with superheated steam, said treatment with superheated steam being continued until said cellulose ester is swollen and the internal stresses in the yarns are released and the dimensions of the fabric are stabilized to subsequent washing, the time and temperature of said treatment being insufficient to efiect fusion or coalescence of said yarns, removing the fabric from contact with the superheated steam before the moisture content of said cellulose ester has been reduced below said saturation regain value so that said fabric still carries an excess of water on the surface of said yarns, and cooling the treated fabric, said fabric being supported throughout substantially its entire area while it is subjected to the superheated steam.
  • a process for improving the dimensional stability of knitted fabric containing yarns of cellulose acetate having a saturation regain value at 100 C. of about 14 to 16% which comprises subjecting said knitted fabric, wetted with at least 50% of water, based on the weight of the dried fabric to superheated steam having a temperature above about 230 F., maintaining said fabric at a definite width and at a moisture content above the saturation regain value of said cellulose ester through out the treatment with superheated steam, said treatment with superheated steam being continued until said cellulose ester is swollen and the internal stresses in the yarns are released and the dimensions of the fabric are stabilized to subsequent washing, the time and temperature of said treatment being insufiicient to effect fusion or coalescence of said yarns, removing the fabric from contact with the superheated steam before the moisture content of said cellulose ester has been reduced below said saturation rgain value so that said fabric still carries an excess of water on the surface ofsaid yarns, and cooling the treated fabric, said fabric being supported throughoutsubstant
  • a process for improving the dimensional stability of knitted fabric containing cellulose acetate yarns which comprises subjecting said knitted fabric, wetted with at least 20% of water based on the weight of the dried fabric, to superheated steam having a temperature above about 230 F., maintaining said fabric at a definite width and at a moisture content above the saturation regain value of said cellulose ester throughout the treatment with superheated steam, said treatment with superheated steam being continued until said cellulose ester is swollen and the internal stresses in the yarns are released and the dimensions of the fabric are stabilized to subsequent washing, the time and temperature of said treatment being insufficientto effect fusion or coalescence of said yarns, removing the fabric from contact with the superheated steam before the moisture content of said cellulose ester has been reduced below said saturation regain value so that said fabric still carries an excess of water on the surface of said yarns, and cooling the treated fabric, said fabric being supported throughout substantially its entire area while it is subjected to the superheated steam, said superheated steam being applied to both the
  • a process for improving the dimensional stability of knitted fabric containing a thermoplastic lower aliphatic acid ester of cellulose yarns which comprises subjecting said knitted fabric, wetted with at least 20% of water based on the weight of the dried fabric, to superheated steam having a temperature above about 230 F, maintaining said fabric at a definite width and at a moisture content above the saturation regain value of said cellulose ester throughout the treatment with superheated steam, said treatment with superheated steam being continued until said cellulose ester is swollen and the internal stresses in the yarns are released and the dimensions of the fabric are stabilized to subsequent washing, the time and temperature of said treatment'being insufiicient to effect fusion or coalescence of saidyarn, removing the fabric from contact with the superheated steam before the moisture content of said cellulose ester has been reduced below said saturation regain value so that said such conditions that the number of wales per.
  • inch of the fabric has been increased, which comprises stretching said fabric to a definite width to decrease the number of wales per inch and subjecting said fabric containing 120%, based on the weight of the dried fabric, of water to superheated steam having a temperature above about 230 F., maintaining said fabric at said definite width and at a moisture content above the saturation regain value of said cellulose ester throughout the treatment with superheated steam, said treatment with superheated steam being continued until said cellulose ester is swollen and the internal stresses, in the yarns are released and the dimensions of the fabric are stabilized to subsequent washing, the time and temperature of said treatment being insuflicient to effect fusion or coalescence of said yarns, removing the fabric from contact with the superheated steam before the moisture content of said cellulose ester-has been reduced below said saturation regain value so that said fabric still carries an excess of water on the surface of said yarns, and cooling the treated fabric, said fabric being supported throughout substantially its entire area while it is subjected to the superheated steam.
  • a continuous process for improving the dimensional stability of warp knitted fabric containing cellulose acetate yarns after said fabric has been subjected to hot Water under such conditions that the number of wales per inch of the fabric has been increased which comprises continuously stretching said fabric to a definite width to decrease the number of wales per inch and continuously subjecting said fabric containing 50120%, based on the weight of the dried fabric, of water to superheated steam having a temperature above about 230 F., maintaining said fabric at said definite width and at a moisture content above the saturation regain value of said cellulose ester throughout the treatment with superheated steam, said treatment with superheated steam being continued until said cellulose ester is swollen and the internal stresses in the yarns are released and the dimensions of the fabric are stabilized to subsequent washing, the time and temperature of said treatment being insuficient to effect fusion or coalescence of said yarns, continuously removing the fabric from contact with the superheated i steam before the moisture content of said cellulose ester has been reduced below said saturation regain value so that

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Description

1957 B. s. SPRAGUE El AL 2,777, 5 PROCESS OF STABILIZING THERMOPLASTIC KNIT-TED FABRIC CONTAINING CELLULOSE ESTER YARNS WITH SUPERHEATED STEAM Filed NOV. 13, 1952 3 Sheets-Sheet 1 w {j m INVENTORS. (\1 v a? v BASIL S.SPRAGUE MURRAY N.CARROLL kn 7 ROBERT H. ROUGHSEDGE I I I 1 I I I ATTORNEYS.
, 2,777,750 FABRIC CONTAINING 5 WITH SUPERHEATED F 19:17 B. s. SPRAGUE ETA].
PROCESS OF STABILIZING THERMOPLASTIC KNITTED CELLULOSE ESTER YARN STEAM Filed Nov. 13, 1952 3, Sheets-Sheet 2 E I \N .1 \N .EOD Iv .5 RE I RGRS S AA H TRCG N WNW m u i 19 za R J m mH m Q N N mm N. mw In. 1| III 8 Pl 4F 1 1|. 1 PH 1 ll 1 1 1 d Ill R Q d u N N1 u N N. v 4 M P1 mm mm 8 l m N 3 i w J a 5 mm d- H 1 E mm A o a @N M +N 3 a 3 WM 1957 I B. s. SPRAGUE ETAI. ,7 7,
PROCESS OF STABILIZING THERMOPLASTIC KNITTED FABRIC CONTAINING CELLULOSE ESTER YARNS WITH SUPERHEATED STEAM Filed Nov. 13, 1952 v 3 Sheets-Sheet 3 INVENTORS. BASIL S. SPRAGUE' MURRAY N. CARROLL V ROBERT H- ROUGHSEDGE BY (W ATTORNEYS.
United States PROCESS OF STABILlZING THERMUPLASTIC KNITTED FABRIC (IONTAWENG CELLU- ggggESl'ER YARNS WITH SUPEREATED 9 Claims. (Cl. 8-131) 62.3265.- N. 3., New
This invention relates to the treatment of textile fabrics and relates more particularly to a process and apparatus for the treatment of knitted fabrics containing yarns of cellulose acetate or other organic acid esters of cellulose.
It has long been known that knitted fabrics contm'ning yarns of cellulose acetate or other organic acid esters of cellulose exhibit a certain degree of dimensional instability when subjected to laundering processes. When garments made of Warp knitted cellulose acetate are laundered in water at 140 F. and then dried Without stretching, their dimensions may change as much as 30% in width and 10% in length, the length direction denoting the direction in which the fabric is fort. ed during knitting. The extent of such dimensional change depends, in part, on the manner in which the garment is finished after laundering, i. e. ironing or pressing. Mainly, however, the extent of dimensional change depends on the previous treatment of the fabric, for example the treatment of the fabric during and after the scouring and dyeing operations. Customarily these scouring and dyeing operations are conducted in hot aqueous baths. If the wet knitted fabric leaving such baths is dried without stretching, the resulting fabric is commercially unacceptable for most uses, since the wales of the fabric are drawn together and are directly in contact with one another, thereby greatly reducing the width of the fabric. Accordingly, it has been customary to treat the wet fabric coming from the dyeing operation by stretching it on a tenter frame and drying it, while stretched, to a low moisture content, such as a moisture content of less than 6% based on the bone dry weight of the fabric, i. e. less than 6% regain. This process introduces internal stresses into the yarns comprising the knitted fabric, and when the fabric is laundered, or subjected to other Wetatnt ting and mechanical working treatment, the fabric tends to return to its former configurations and dimensions. Such dimensional change is manifestly undesirable.
It is an important object of this invention to provide a process and apparatus for the treatment of knitted fabrics containing yarns of cellulose acetate or other organic acid esters of cellulose which will overcome the foregoing and other difiiculties and which will be especially efiicient in operation.
A further object of this invention is the provision of a process and apparatus for the treatment of knitted fabrics containing yarns of cellulose acetate or other organic acid esters of cellulose which will impart to said fabrics a high degree of dimensional stability.
Other objects of this invention, together with certain details of construction and combinations of parts of the apparatus, will be apparent from the following detailed description and claims.
According to the present invention, a knitted fabric containing yarns of cellulose acetate or other organic acid esters of cellulose carrying a film of liquid water is raised to an elevated temperature in a gaseous atmoswhile the fabric is held to phere, preferably of steam,
fabric is supported througha definite width and while the out substantially its entire area. The wet fabric is maintained at the elevated temperature until the cellulose acetate or other organic acid ester of cellulose of which the yarns are composed is swollen and any internal stresses in the yarns are released, but care should be taken so as not to cause the yarns or the fibers making up the yarns to fuse or coalesce one with the other. During this treatment the moisture content of the fabric should not fall below its saturation regain value, which is defined as the moisture regain value of the fabric in contact with an atmosphere of relative humidity at the temperature of the fabric. The fabric is cooled and, if desired, dried. Following this treatment, it is found that the fabric exhibits a high degree of dimensional stability so that garments made of said fabric will, from a practical viewpoint, retain their shape and dimensions substantially unchanged during normal use.
In our preferred procedure, a wet knitted fabric of cellulose acetate is subjected to superheated steam, and the moisture content of the fabric before contact with the superheated steam and the time of contact with the superheated steam are so regulated that the excess surface moisture on the fabric is not completely evaporated and the moisture content of the fabric does not fall below its saturation regain value. That is, despite the evaporation of some of the water due to the drying effect of the superheated steam, an excess of water is maintained on the surface of the yarns throughout the exposure to the superheated steam. Thepresence of this excess of water is critical. If the moisture content of the fabric is below the 100 C. saturation regain value when it is first placed into contact with the superheated steam, adequate dimensional stability will not be obtained. if, on the other hand, through evaporation the moisture content drops below the saturation regain value during contact with the superheated steam the yarns of cellulose acetate will deluster.
Since the 100 C. saturation regain value of cellulose acetate yarns is generally about 14% to 16%, the fabric advantageously should have a water content prior to steam treatment of at least about 20% by weight, preferably at least 50% byweight, based on the weight of the dried fabric, to insure that the water content of all portions of the fabric is above the minimum value, thereby avoiding dry spots whose dimensional stability will differ from that of the remainder of the treated fabric. The maximum water content of the fabric should normally not exceed about by weight to avoid the necessity of heating large quantities of water to an elevated temperature during the steam treatment. Moreover, it is difficult to distribute such larger quantities of water in a uniform manner throughout the fabric before the treatment with steam. The presence of uniformly distributed larger quantities of water in the fabric will, however, not interfere with the successful treatment of the fabric to impart a high degree of dimensional stability thereto. The desired amount of water may be added to a dry knitted fabric to prepare it for treatment in accordance with the process of this invention. Commercially, however, the process is best applied to the fabric immediately following the final liquid treatment constituting a step in the finishing of the fabric. For example, the fabric in its wet condition following a wet finishing treatment is first treated to reduce its water content to the desired level, as by centrifuging, and then stretched by about 5 to 30% to a definite width before being subjected to the heat treatment in the manner set forth above. Not only does carrying out the process of this invention following the final liquid treatment in the finishing of the fabric effect important economies, but it also produces a fabric having the highest degree of dimensional stability since the said 3 fabric is not subjected to any further stresses while in a hot, wet state before it is processed into garments. If desired, the knitted cellulose ester fabric while being stabilized may have thereon any of the softening and antistatic, finishes usually applied to such fabrics.
As stated, the wet fabric is treated, in accordance with this invention, with steam while it is held to a definite width and while it is supported throughout substantially its entire area. One form of apparatus for carrying out this treatment comprises a chamber provided with an inlet and exit slot, through Which the fabric enters and leaves the chamber, and equipped with tenter chains for holding the fabric to a definite width and moving the fabric continuously through the chamber. There are also provided in the chamber, between the tenter chains, a plurality of rubber covered rollers for supporting the fabric throughout substantially its entire area. The rollers are positively driven'so as to have a peripheral speed substantially equal to the linear speed of the fabric moving through the chamber so that no stresses will be applied to said fabric. Instead of rollers, other means such as screens, belts or the like may be used to support the fabric during the treatment. As the fabric moves through the chamber it is treated with steam which is advantageously introduced into the chamber through distributing heads positioned both above and below the fabric at a plurality of points spaced along the path of the fabric. The steam raises the temperature of the fabric to a point where the wet cellulose acetate or other organic acid ester of cellulose comprising the yarns of the fabric is swollen and in a condition in which the internal stresses in the yarns are released rapidly. This temperature is preferably about 100 C. The steam treatment should, however, not be continued to a point where the yarns or the fibers making up the yarn tend to coalesce or where the hand of the fabric in changed in an undesirable manner. It is essential that the fabric be supported throughout its entire area while it is at this elevated temperature. If no such support is provided, the fabric will tend to sag and be distorted due to its weight, thereby introducing stresses which will be locked into the fabric during the treatment and will cause dimensional changes in the fabric during use.
The superheated steam, which is desirably at atmospheric pressure and at a temperature above about 230 F.', preferably in the range of about 240 F. to 250 F., is admitted to the chamber through a plurality of openings. The spacing of the openings throughout the chamber is such that there is obtained an even distribution of steam throughout the area of the chamber. Moreover, the entering steam is caused to impinge on the fabric at fairly high velocity so as to effect an efiicient transfer of heat to the fabric. In addition, a very even-steam distribution is necessary because of the previously described hazard of delustering which occurs if the fabric is over dried at any point during passage through the stabilization chamber. The waste steam is exhausted from the chamber by means of exhaust ducts mounted at the side of the chamber. 7
- In order to prevent the inrush of cool atmospheric air to the chamber, the exhaust rate is adjusted so that the rate of removal of spent steam at the exhaust ducts does not quite balance the input rate. That is, more steam is admitted to the chamber than is removed through the exhaust ducts. Hence, during operation a small amount of steam escapes through the slots through which the fabric enters and leaves the chamber. In addition, these exit and inlet slots have mounted, above and below, slotted. conduits through which heated air is forced. These conduits are mounted and aligned so that the heated air from the slots forms an air curtain through which the fabric passes. This air curtain further serves to dilute the-escaping steam and prevent condensation on the surrounding equipment. If desired, the wet fabric may be preheated in any desired manner to an elevated temperature below the stabilizing treatment temperature prior to its entry into the chamber so as to reduce the period of time needed for the steam to bring the fabric to the treatment temperature. The time of treatment varies, depending upon alarge number of factors, including the percentage of water present initially in the fabric, the temperature at which the Wet fabric enters the chamber, the weight of the fabric, the steam temperature, the degree of suprheat and the like. Control of the time of treatment is effected by adjusting the rate at which the fabric passes through the chamber, that is, by regu lating the speed of the tenter chains.
Following the steam treatment, the fabric is cooled. At least during the preliminary stages of the cooling, the fabric should be held to a definite width and supported throughout its entire area so as to avoid imposing stresses upon the hot fabric. Cooling may be eifected simply by passing the fabric through the air, or, if desired, the rate of cooling may be accelerated by passing a stream of cool air over the fabric.
During the treatment of the wet fabric with superheated steam, at least a portion ofthe water in the fabric will be driven oif. After the cooling of the fabric is completed, any further drying of the fabric that may be necessary is carried out by passing the fabric through a dryer of any desired type. It is preferred to reduce the moisture content of the cellulose acetate to about 5 to 7% regain. Over-drying tends to impart an objectionably harsh hand to the fabric. The dried fabric exhibits a high degree. of dimensional stability and is eminently suited for a Wide variety of applications.
A preferred embodiment of the 'apparatusof this invention is shown in the accompanying drawings wherein: Fig. 1 is a side view of the apparatus, partly in section, Fig. 2 is a cross-sectional view of the apparatus, taken on the line 2-2 in Fig. l, in the direction of the arrows, Fig. 3 is a cross-sectional view of the apparatus, taken on the line 3-3 in Fig. l, in the direction of the arrows, Fig. 4 is a detail view of the upper steam distributor, and
Fig. 5 is a detail view of the lower steam distributor. Referring now to the drawing, the reference numeral 11 designates a fabric whose edges are secured to tender chains 12 that act to hold the fabric at a definite width. The tenter chains 12 are mounted on supports, indicated generally by reference numeral 13, that may be operated by means of hand wheeis 14 to adjust the lateral spacing between the tenter chains 12 in'a manner Well known in the art. The tenter chains 12 carry the fabric 11 between a pair of heaters 15 equipped with infra-red heating elements to effect a preheating of the said fabric. The
I fabric 11 is then moved by the tenter chains 12 into a 'treating chamber, indicated generally by reference numeral 16. The treating chamber 16 comprises a shell 17 that is supported on. a framework 18. The top 19 and upper portion of the ends 21 of the shell 17 are of double wall construction and a heating fluid such as steam is passed through said walls to raise them to an elevated temperature so that no water will condense on said walls to drop onto the fabric 11. Positioned in the chamber 16 are a plurality of rubbe covered rolls 22 that extend transversely of the chamber between the tenter chains 12 and act to support the fabric during its treatment. The rolls 22 are driven at a peripheralspeed equal to the linear speed of the tenter chains 12 by means of a motor 23 through a variable speed drive 24, a chain 25 and a series ofchains 26 and sprockets 27 that act to interconnectall'said rolls. Steam is introduced into the chamber 16 through a plurality of lower distributors, indicated generally by reference nu-. meral 28, that are positioned between the rolls 22 beneath the fabric 11, and a plurality of upper distributors, indicated generally by reference numeral 29, that :are positioned above the fabric 11. 7 i
"Each of the lower distributors 28 -compnses a conduit 31 supported on a pedestal 32 (Fig. and having, a slot 33 extending through the uppermostportion thereof for the discharge of the steam which is supplied to-said lower distributors from headers 34. The upper distributors 29 each comprises an elongated rectangular enclosure 35 to which steam is supplied by headers 36 through conduits 37. Extending longitudinally of the enclosure 35 are partitions 38 having apertures 39 therein which act to distribute the steam emerging from the conduits 37 more uniformly. To insure that there will be no drops of water in the steam emerging from the upper distributors 29 to fall on and spot the fabric 13, there are provided a pair of conduits 41 extending the full length of the enclosure 35 and being spaced apart a short distance to provide a passageway 42 therebetween. A heating fluid, such as steam, which may be at a higher temperature than the steam in the headers 36, is introduced into the conduits .1 from a header 43 and is discharged from said conduits through a header 44. All the steam flowing through the passageway 42 will come into intimate contact with the heated surfaces of the conduits 41. thereby turning into steam any drops of water that may be present in the steam emerging from the headers 36. Moreover, when the steam which is at super-atmospheric pressure in the headers 34 and 36 enters the chamber 15, which is at approximately atmospheric pressure, the essentially adiabatic drop in the pressure of the steam will impart a degree of superheat thereto and tend to eliminate water droplets therefrom.
If atmospheric air were permitted to enter into the chamber 16 freely together with the fabric 11, there would be a tendency for the cold atmospheric air to cause water to condense on all surfaces adjacent the entrance passageway. To avoid this possibility, there are provided adjacent the entrance and exit passageways pairs of conduits 45 and 45 having slots 46 and 46' therein that face toward the fabric 11. Heated air under pressure is introduced into the conduits 45 and 45' and flows through the slots 46 and 46' toward the fabric 11 thereby acting as an air curtain to prevent the flow of cold atmospheric air into the chamber 16 and also acting to assist in the preheating of the said fabric. The chamber 16 is provided with exhaust ducts 47 through which pass a constant flow of steam together with any air that may enter into the chamber during operation.
Upon leaving the chamber 16, the fabric 11 passes through a cooling section, indicated generally by reference numeral 48. in at least the first portion of the cooling section 48, the fabric 11 is held at a definite width and. supported throughout substantially its entire area in the same manner as during its passage through the chamber 16, namel by the tenter chains 12 and rolls 22. Cooling of the fabric 11 may be effected simply through the action of atmospheric air. However, if desired, means such as slotted conduits, fans or the like may be provided for producing a forced flow of a cooling medium, such as air, over the fabric 11 and, if even more rapid cooling is desired, the cooling medium may be refrigerated.
The fabric 11, after cooling, is carried by the tenter chains 1: into a dryer 49 of any type. Means may be provided for supporting the fabric throughout its entire area as it passes through the dryer 49, although this has been found unnecessary when the drying conditions are not severe. When the temperature and other drying conditions are such as to reduce the moisture content below about 4% regain, such supporting means is desirable to prevent the introduction of a small, but not highly objectionable, degree of dimensional instability into the fabric 11. if the drying conditions are not so severe and fabric supporting means are not employed in the drier, the lateral spacing between the tent-er chains 12 may be widened slightly, e. g. by about 4%, as these chains pass through the drier, in order to avoid any substantial sagging of the fabric in the drier. a
p The following example is givento illustrate in.- vention further.
Example- A large number ofpieces of fabric warp knittedof 55 denier yarns of cellulose acetate having an acetyl value of 54.5%, measured as combined acetic acid, are scoured, dyed and washed and are then centrifuged to bring their moisture content to about based on the dry weight of the fabric. The wet fabrics, which are at room ternperature and have a width of about 90 inches, are sewn end to end and are then passed one after another through the apparatus shown in the drawings, without using preheater 15, at the rate of about 1300 pounds of wet fabric per hour while the fabrics are maintained at a width of ill inches and while saturated steam at: a pressure of 150 pounds per square inch gauge is passed at therate of about 5,000 pounds per hour through a throttling valve (not shown), through which it expands in an essentially adiabatic manner into the conduits leading to the lower distributors 28, upper distributors 29 and conduits 41. The overall temperature of the treating chamher is above 230 F. After a treatment time of 15 seconds, the fabric is cooled and dried. The dried fabrics, when laundered in an automatic washer at F. and dried in substantially tensionless condition, exhibit an average area shrinkage of less than 4%. Subsequent laundering efiects no appreciable change in dimensions. When similar pieces of the same fabric are finished and dried in conventional manner they exhibit an average area shrinkage of 15% to 30% after the first washing.
While the process of this invention has been described specifically in connection with the treatment of fabrics containing cellulose acetate yarns at the present time, it may also be employed for the treatment of the fabrics containing yarns of othr organic acid esters of cellulose such as, for example, cellulose propiouate, cellulose butyrate, cellulose acetate propionate and cellulose acetate butyrate.
it is to be understood that the foregoing detaileddescription is given merely by way of illustration and'that many variations may be made therein without departing from the spirit of our invention.
Having described our invention, What We desire to se' cure by Letters Patent is:
l. A process for improving the dimensional stability of knitted fabric containing a thermoplastic lower aliphatic acid ester of cellulose yarns which comprises subjecting said knitted fabric, wetted with at least 20% of water based on the weight of the dried fabric, to superheated steam having a temperature above about 233 F, maintaining said fabric at a definite width and at a moisture content above the saturation regain value of said cellulose ester throughout the treatment'with superheated steam, said treatment with superheated'steam being continued until said cellulose ester is swollen and the internal stresses in the yarns are released and the dimensions of the fabric are stabilized to subsequent washing, the time and temperature of said treatment being insuiicient to efiect fusion or coalescence of said yarns, removing the fabric from contact with the superheated steam before the moisture content of said cellulose ester has been reduced below said saturation regain value so that said fabric still carries an excess of water on the surface of said yarns, and cooling the treated fabric, said fabric being supported throughout substantially its entire area while it is subjected to the superheated steam.
2. A process for improving the dimensional stability of knitted fabric containing cellulose acetate yarns which comprises subjecting said knitted fabric, wetted with at least 20% of Water based onthe weight of the dried fabric, to superheated steam having a temperature above about 230 F., maintaining said fabric at adefinite width and at a moisture content above the saturation regain value of said cellulose ester throughout the treatment with superheated steam, said treatment with superheated steam being continued until said cellulose ester is swollen and the internal stresses in the yarns are released and the dimensions of the fabric are stabilized to subsequent washing, the time and temperature of said treatment being insufficient to efiect fusion or coalescence of said yarns, removing the fabric from contact with the superheated steam before the moisture content of said cellulose ester has been reduced below said saturation regain value so that said fabric still carries an excess of water on the surface of said yarns, and cooling the treated fabric, said fabric being supported throughout substantially its entire area while it is subjected to the superheated steam.
3. A process for improving the dimensional stability of knitted fabric containing yarns of cellulose acetate having a saturation regain value at 100 C. of about 14 to 16% which comprises subjecting said knitted fabric, wetted with at least 50% of water, based on the weight of the dried fabric to superheated steam having a temperature above about 230 F., maintaining said fabric at a definite width and at a moisture content above the saturation regain value of said cellulose ester through out the treatment with superheated steam, said treatment with superheated steam being continued until said cellulose ester is swollen and the internal stresses in the yarns are released and the dimensions of the fabric are stabilized to subsequent washing, the time and temperature of said treatment being insufiicient to effect fusion or coalescence of said yarns, removing the fabric from contact with the superheated steam before the moisture content of said cellulose ester has been reduced below said saturation rgain value so that said fabric still carries an excess of water on the surface ofsaid yarns, and cooling the treated fabric, said fabric being supported throughoutsubstantially its entire area while it is subjected to the superheated steam.
4. A process for improving the dimensional stability of knitted fabric containing cellulose acetate yarns which comprises subjecting said knitted fabric, wetted with at least 20% of water based on the weight of the dried fabric, to superheated steam having a temperature above about 230 F., maintaining said fabric at a definite width and at a moisture content above the saturation regain value of said cellulose ester throughout the treatment with superheated steam, said treatment with superheated steam being continued until said cellulose ester is swollen and the internal stresses in the yarns are released and the dimensions of the fabric are stabilized to subsequent washing, the time and temperature of said treatment being insufficientto effect fusion or coalescence of said yarns, removing the fabric from contact with the superheated steam before the moisture content of said cellulose ester has been reduced below said saturation regain value so that said fabric still carries an excess of water on the surface of said yarns, and cooling the treated fabric, said fabric being supported throughout substantially its entire area while it is subjected to the superheated steam, said superheated steam being applied to both the upper and lower surfaces of said fabric.
5. A process for improving the dimensional stability of knitted fabric containing a thermoplastic lower aliphatic acid ester of cellulose yarns which comprises subjecting said knitted fabric, wetted with at least 20% of water based on the weight of the dried fabric, to superheated steam having a temperature above about 230 F, maintaining said fabric at a definite width and at a moisture content above the saturation regain value of said cellulose ester throughout the treatment with superheated steam, said treatment with superheated steam being continued until said cellulose ester is swollen and the internal stresses in the yarns are released and the dimensions of the fabric are stabilized to subsequent washing, the time and temperature of said treatment'being insufiicient to effect fusion or coalescence of saidyarn, removing the fabric from contact with the superheated steam before the moisture content of said cellulose ester has been reduced below said saturation regain value so that said such conditions that the number of wales per. inch of the fabric has been increased, which comprises stretching said fabric to a definite width to decrease the number of wales per inch and subjecting said fabric containing 120%, based on the weight of the dried fabric, of water to superheated steam having a temperature above about 230 F., maintaining said fabric at said definite width and at a moisture content above the saturation regain value of said cellulose ester throughout the treatment with superheated steam, said treatment with superheated steam being continued until said cellulose ester is swollen and the internal stresses, in the yarns are released and the dimensions of the fabric are stabilized to subsequent washing, the time and temperature of said treatment being insuflicient to effect fusion or coalescence of said yarns, removing the fabric from contact with the superheated steam before the moisture content of said cellulose ester-has been reduced below said saturation regain value so that said fabric still carries an excess of water on the surface of said yarns, and cooling the treated fabric, said fabric being supported throughout substantially its entire area while it is subjected to the superheated steam.
7. A continuous process for improving the dimensional stability of warp knitted fabric containing cellulose acetate yarns after said fabric has been subjected to hot Water under such conditions that the number of wales per inch of the fabric has been increased, which comprises continuously stretching said fabric to a definite width to decrease the number of wales per inch and continuously subjecting said fabric containing 50120%, based on the weight of the dried fabric, of water to superheated steam having a temperature above about 230 F., maintaining said fabric at said definite width and at a moisture content above the saturation regain value of said cellulose ester throughout the treatment with superheated steam, said treatment with superheated steam being continued until said cellulose ester is swollen and the internal stresses in the yarns are released and the dimensions of the fabric are stabilized to subsequent washing, the time and temperature of said treatment being insuficient to effect fusion or coalescence of said yarns, continuously removing the fabric from contact with the superheated i steam before the moisture content of said cellulose ester has been reduced below said saturation regain value so that said fabric still carries an excess of Water on the surface of said yarns, and continuously cooling the treated fabric, said fabric being supported throughout substantially its entire area whiie it is subjected to the superheated steam.
8. Process asset forth in claim 7 in which said cellulose acetate has a saturation regain value at C. of about 14 to 16% and the water content of said fabric just before it is subjected to the superheated steam is at least 50%, based on the weight of the dried fabric.
9. Process as set forth in claim Sin which said fabric is supported throughout substantially its entire area dur- (References on following page) References Cited in the file of this patent UNITED STATES PATENTS Spooner July 16, 1935 Croft Mar. 25, 1941 Wedler Mar. 7, 1944 Benger Dec. 26, 1944 Vincent et a1. Jan. 17, 1950 10 Helmus Feb. 28, 1950 Dodge Oct. 10, 1950 OTHER REFERENCES Nisbet: American Dyestutf Reporter, October 31, 1949, pp. 773, 774.
Rayon and Synthetic Textiles, August 1950, p, 62.

Claims (1)

  1. 6. A PROCESS FOR IMPROVING THE DIMENSIONAL STABILITY OF WARP KNITTED FABRIC CONTAINING CELLULOSE ACETATE YARNS AFTER SAID FABRIC HAS BEEN SUBJECTED TO HOT WATER UNDER SUCH CONDITIONS THAT THE NUMBER OF WALES PER INCH OF THE FABRIC HAS BEEN INCREASED, WHICH COMPRISES STRETCHING SAID FABRIC TO A DEFINTE WIDTH TO DECREASE THE NUMBER OF WALES PER INCH AND SUBJECTING SAID FABRIC CONTAINING 50-120%, BASED ON THE WEIGHT OF THE DRIED FABRIC, OF WATER TO SUPERHEATED STEAM HAVING A TEMPERATURE ABOVE ABOUT 230*F., MAINTAINING SAID FABRIC AT SAID DEFINITE WIDTH AND AT A MOISTURE CONTENT ABOVE THE SATURATION REGAIN VALUE OF SAID CELLULOSE ESTER THROUGHOUT THE TREATMENT WITH SUPERHEATED STEAM, SAID TREATMENT WITH SUPERHEATED STEAM BEING CONTINUED UNTIL SAID CELLULOSE ESTER IS SWOLLEN AND THE INTERNAL STRESSES IN THE YARNS ARE RELEASED AND THE DIMENSIONS OF THE FABRIC ARE STABILIZED TO SUBSEQUENT WASHING, THE TIME AND TEMPERATURE OF SAID TREATMENT BEING INSUFFICIENT TO EFFECT FUSION OR COALESCENCE OF SAID YARNS, REMOVING THE FABRIC FROM CONTACT WITH THE SUPERHEATED STEAM BEFORE THE MOSITURE CONTENT WITH THE CELLULOSE ESTER HAS BEEN REDUCED BELOW SAID SATURATION REGAIN VALUE SO THAT SAID FABRIC STILL CARRIES AN EXCESS OF WATER ON THE FURFACE OF SAID YARNS, AND COOLING THE TREATED FABRIC, SAID FABRIC BEING SUPPORTED THROUGHOUT SUBSTANSTEAM.
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Cited By (13)

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US2973635A (en) * 1956-03-23 1961-03-07 American Viscose Corp Apparatus for finishing textiles
US2993749A (en) * 1958-05-23 1961-07-25 William G Sloan Cellulose esters with dimensional stability
US3101236A (en) * 1954-12-02 1963-08-20 Celanese Corp Textile treating
US3318114A (en) * 1964-08-14 1967-05-09 Pottsville Bleaching And Dyein Method and apparatus for setting the color of dyed tubular fabrics
US3445902A (en) * 1965-12-13 1969-05-27 Beloved Toys Inc Method and apparatus for reconditioning pile fibers
US3447346A (en) * 1965-11-09 1969-06-03 Norton Co Ltd Sir James Farmer Steam treating apparatus
US3712086A (en) * 1971-10-26 1973-01-23 Mc Graw Edison Co Apparatus for producing a durable press in garments containing cellulose or cellulosic derivatives
US3973417A (en) * 1973-06-06 1976-08-10 Burlington Industries, Inc. Apparatus for thermosol dyeing of polyester fabrics
US4742697A (en) * 1985-08-07 1988-05-10 Sando Iron Works Co., Ltd. Apparatus for continuous wet heat treatment of a cloth
US4744160A (en) * 1986-09-10 1988-05-17 Astechnologies, Inc. Fabric pressing machine using superheated steam
US5311754A (en) * 1990-08-07 1994-05-17 Eduard Kusters Maschinenfabrik Gmbh & Co. Kg Steam-filled treatment chamber
US5634226A (en) * 1993-04-03 1997-06-03 Sandoz Ltd. Apparatus and process for the continuous dyeing of mesh material
US20190169776A1 (en) * 2017-12-04 2019-06-06 Superba S.A.S. Heat distribution management device for wire treatment

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US2008230A (en) * 1933-06-06 1935-07-16 Spooner William Wycliffe Steaming of webs of material
US2235869A (en) * 1939-03-14 1941-03-25 Celanese Corp Treatment of fabrics
US2343351A (en) * 1942-02-26 1944-03-07 American Viscose Corp Method and apparatus for modifying textile fabrics
US2365931A (en) * 1941-02-13 1944-12-26 Du Pont Finishing of polyamide fabrics
US2494731A (en) * 1945-06-26 1950-01-17 Olin Mathieson Apparatus for steaming textiles
US2499142A (en) * 1948-07-14 1950-02-28 Fair Lawn Finishing Company Heat setting of textile fabrics
US2524895A (en) * 1945-10-31 1950-10-10 Celanese Corp Puckering a thermoplastic fabric by heating one side thereof

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* Cited by examiner, † Cited by third party
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US2008230A (en) * 1933-06-06 1935-07-16 Spooner William Wycliffe Steaming of webs of material
US2235869A (en) * 1939-03-14 1941-03-25 Celanese Corp Treatment of fabrics
US2365931A (en) * 1941-02-13 1944-12-26 Du Pont Finishing of polyamide fabrics
US2343351A (en) * 1942-02-26 1944-03-07 American Viscose Corp Method and apparatus for modifying textile fabrics
US2494731A (en) * 1945-06-26 1950-01-17 Olin Mathieson Apparatus for steaming textiles
US2524895A (en) * 1945-10-31 1950-10-10 Celanese Corp Puckering a thermoplastic fabric by heating one side thereof
US2499142A (en) * 1948-07-14 1950-02-28 Fair Lawn Finishing Company Heat setting of textile fabrics

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3101236A (en) * 1954-12-02 1963-08-20 Celanese Corp Textile treating
US2973635A (en) * 1956-03-23 1961-03-07 American Viscose Corp Apparatus for finishing textiles
US2993749A (en) * 1958-05-23 1961-07-25 William G Sloan Cellulose esters with dimensional stability
US3318114A (en) * 1964-08-14 1967-05-09 Pottsville Bleaching And Dyein Method and apparatus for setting the color of dyed tubular fabrics
US3447346A (en) * 1965-11-09 1969-06-03 Norton Co Ltd Sir James Farmer Steam treating apparatus
US3445902A (en) * 1965-12-13 1969-05-27 Beloved Toys Inc Method and apparatus for reconditioning pile fibers
US3712086A (en) * 1971-10-26 1973-01-23 Mc Graw Edison Co Apparatus for producing a durable press in garments containing cellulose or cellulosic derivatives
US3973417A (en) * 1973-06-06 1976-08-10 Burlington Industries, Inc. Apparatus for thermosol dyeing of polyester fabrics
US4742697A (en) * 1985-08-07 1988-05-10 Sando Iron Works Co., Ltd. Apparatus for continuous wet heat treatment of a cloth
US4744160A (en) * 1986-09-10 1988-05-17 Astechnologies, Inc. Fabric pressing machine using superheated steam
US5311754A (en) * 1990-08-07 1994-05-17 Eduard Kusters Maschinenfabrik Gmbh & Co. Kg Steam-filled treatment chamber
US5634226A (en) * 1993-04-03 1997-06-03 Sandoz Ltd. Apparatus and process for the continuous dyeing of mesh material
US20190169776A1 (en) * 2017-12-04 2019-06-06 Superba S.A.S. Heat distribution management device for wire treatment
US11519115B2 (en) * 2017-12-04 2022-12-06 Superba Sas Heat distribution management device for yarn treatment

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