US3921420A - Apparatus for wet processing of textile materials - Google Patents

Apparatus for wet processing of textile materials Download PDF

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Publication number
US3921420A
US3921420A US381268A US38126873A US3921420A US 3921420 A US3921420 A US 3921420A US 381268 A US381268 A US 381268A US 38126873 A US38126873 A US 38126873A US 3921420 A US3921420 A US 3921420A
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United States
Prior art keywords
kier
strand material
jet
strand
leg
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Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
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US381268A
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English (en)
Inventor
Christoph W Aurich
James Keith Turner
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Gaston County Dyeing Machine Co
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Gaston County Dyeing Machine Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Gaston County Dyeing Machine Co filed Critical Gaston County Dyeing Machine Co
Priority to US381268A priority Critical patent/US3921420A/en
Priority to CA186,980A priority patent/CA1007009A/en
Priority to GB5562973A priority patent/GB1430279A/en
Priority to DE2360436A priority patent/DE2360436A1/de
Priority to CH1698473D priority patent/CH1698473A4/xx
Priority to CH1698473A priority patent/CH593374B5/xx
Priority to IT1740/73A priority patent/IT1005527B/it
Priority to DD175441*A priority patent/DD107605A5/xx
Priority to FR7345466A priority patent/FR2214248A5/fr
Priority to JP49004587A priority patent/JPS4994979A/ja
Priority to ES421783A priority patent/ES421783A1/es
Priority to NL7317743A priority patent/NL7317743A/xx
Priority to US05/616,152 priority patent/US4001945A/en
Application granted granted Critical
Publication of US3921420A publication Critical patent/US3921420A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06B—TREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
    • D06B15/00—Removing liquids, gases or vapours from textile materials in association with treatment of the materials by liquids, gases or vapours
    • D06B15/09—Removing liquids, gases or vapours from textile materials in association with treatment of the materials by liquids, gases or vapours by jets of gases
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06B—TREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
    • D06B19/00—Treatment of textile materials by liquids, gases or vapours, not provided for in groups D06B1/00 - D06B17/00
    • D06B19/0088—Treatment of textile materials by liquids, gases or vapours, not provided for in groups D06B1/00 - D06B17/00 using a short bath ratio liquor
    • D06B19/0094—Treatment of textile materials by liquids, gases or vapours, not provided for in groups D06B1/00 - D06B17/00 using a short bath ratio liquor as a foam
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06B—TREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
    • D06B3/00—Passing of textile materials through liquids, gases or vapours to effect treatment, e.g. washing, dyeing, bleaching, sizing, impregnating
    • D06B3/28—Passing of textile materials through liquids, gases or vapours to effect treatment, e.g. washing, dyeing, bleaching, sizing, impregnating of fabrics propelled by, or with the aid of, jets of the treating material
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06P—DYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
    • D06P1/00—General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed
    • D06P1/96—Dyeing characterised by a short bath ratio
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06P—DYEING OR PRINTING TEXTILES; DYEING LEATHER, FURS OR SOLID MACROMOLECULAR SUBSTANCES IN ANY FORM
    • D06P1/00—General processes of dyeing or printing textiles, or general processes of dyeing leather, furs, or solid macromolecular substances in any form, classified according to the dyes, pigments, or auxiliary substances employed
    • D06P1/96—Dyeing characterised by a short bath ratio
    • D06P1/965—Foam dyeing
    • D—TEXTILES; PAPER
    • D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
    • D06B—TREATING TEXTILE MATERIALS USING LIQUIDS, GASES OR VAPOURS
    • D06B15/00—Removing liquids, gases or vapours from textile materials in association with treatment of the materials by liquids, gases or vapours
    • D06B15/04—Removing liquids, gases or vapours from textile materials in association with treatment of the materials by liquids, gases or vapours by suction
    • D06B15/043—Removing liquids, gases or vapours from textile materials in association with treatment of the materials by liquids, gases or vapours by suction by means of a perforated drum

Definitions

  • ABSTRACT A method and means are provided having particular significance for dyeing textile strand material by circulating such material in a confined space, preferably, under the aspirating influence of jetted inert gas, and applying a treating liquor formulated for effective application at a short liquor ratio, preferably, by metering the same into the gas as it is supplied to produce the aspirating influence. Excellent distribution of the treating liquor throughout the material is obtained in this manner, while spent liquor effluent is materially reduced.
  • the short liquor ratios involved are, in general, of the order at which no liquor exists outside the substrate following distribution of the treating liquor therein.
  • Such previously established processing practice is adapted for effective use in foaming the treating formulation and distributing it evenly through the substrate in accordance with the present invention by arranging to circulate the piece goods under the aspirating influence of jetted inert gas, and metering the treating formulation into the gas as it is supplied to produce the aspirating influence.
  • FIG. 1 is a diagrammatic illustration of a representative apparatus arrangement suited for practicing the present invention
  • FIG. 2 is a further diagrammatic illustration showing an alternate extraction arrangement
  • FIG. 3 is a side elevation of apparatus modified in certain particulars as has been found advantageous in adapting the invention to production use;
  • FIG. 4 is a plan view corresponding to FIG. 3;
  • FIG. 5 is a longitudinal central section of the vertical intake leg of the FIG. 3 apparatus superstructure
  • FIG. 6 is a side elevation of the superstructure junction housing
  • FIG. 7 is a vertical central section corresponding to FIG. 6;
  • FIG. 8 is a longitudinal central section of the inclined discharge leg of the superstructure.
  • FIG. 9 is a schematic diagram of the operating system associated with the FIG. 3 apparatus.
  • FIGS. 1 and 2 of the drawings are used first to illustrate the manner in which the present invention is practiced because the operating principles involved were confirmed through development work with apparatus of this sort. It should be noted, however, that while the illustrated apparatus is arranged for batch operation, and more particularly for handling piece goods in endless rope form, the confirmed operating principles are of general application, so that the apparatus can be arranged as well for handling the piece goods in open width form, or for treating other textile strand material such as tow, or for continuous operation, with equally good results.
  • an inert gas is re ferred to in describing the operating procedure it is meant that the gas is inert with respect to the treating liquor and the material being handled. That is, that the gas has no unwanted reactive or other influence on the liquor or the material.
  • the gas employed will be air, although one that is inert in the strict sense, such as nitrogen, can be used whenever there is reason to do
  • the gas employed will be air, although one that is inert in the strict sense, such as nitrogen, can be used whenever there is reason to do
  • Strand material circulation can, of course, be effected in a variety of ways, as, for example, with a winch system of the sort commonly employed in dye becks or by suitably arranged rolls of various sorts, and any circulation system employed is almost certain to impose the incidental mechanical forces needed to promote even distribution of the treating liquor, but unless the system employed also provides for a sufficiently rapid circulation rate the time required for treating liquor application and distribution can be unreasonably prolonged. It is for this reason that circulation by jetted inert gas is preferred according to the present invention, although it is the rapid circulation rates made possible by circulation in this manner that is of primary significance and any other system capable of producing reasonably comparable circulation rates would also allow application and distribution of the treating liquor in a reasonable time.
  • FIG. 1 diagrams an adapted form of apparatus such as is disclosed and claimed in the previously noted copending application Ser. No. 272,774, a cylindrical pressure vessel or kier being mounted on a suitable base 12 with its cylindrical axis disposed horizontally to form a treating chamber.
  • a kier loading port is provided at 14 through which piece goods may be introduced for processing in endless strand or rope form as indicated at S, and removed after processing.
  • the kier 10 is partitioned in J-box fashion as shown at 16 to form a storage or accumulation means for the greater portion of the piece goods strand S as it is circulated within the kier after being introduced and confined therein.
  • Provision for circulating the strand S during treatment is arranged at a conduit superstructure which includes a vertical intake portion 18 rising from kier 10, a horizontal continuing portion 20, and a terminal discharge portion 22 returning to the kier 10.
  • a driven roll member 26 which may be of the specially covered sort disclosed and claimed in copending application Ser. No. 234,495 for lifting purposes, or of the suction type comparable to that disclosed and claimed in copending application Ser. No. 240,010 to provide for extraction as well as lifting.
  • the vertical intake portion 18 into which the strand S is lifted from kier 10 is situated adjacent the loading port 14 and above the exit end of the J-box storage means 16, and the housing portion 24 at the upper end thereof is formed to enclose the driven roll member 26 at an offset disposition such that the strand S is lifted axially into intake portion 18 by roll member 26 and delivered therefrom axially to the continuing superstructure portion 20.
  • venturi structure 28 is formed in this continuing horizontal portion 20, just beyond roll member 26, a venturi structure 28 is formed. Except for the roll housing portion 24, the other superstructure portions preferably have a lengthwise tubular form that is enough larger in cross section at all points than the strand material S to allow for passage of this material freely therethrough, and the venturi structure 28 is formed by a tapered necking of the horizontal continuing portion 20 at 30 and the installation of a venturi tube 32 thereat.
  • the installed venturi tube 32 is arranged concentrically within the continuing portion 20 so that its downstream end is spaced to provide an annular nozzle at the necking 30 that is fed through a piping connection at 32.
  • the upstream end of venturi tube 32 is flared to receive strand material S delivered by the roll member 26 readily, and is adjacently sealed within the continuing superstructure portion 20 so that the feed through piping connection 34 can escape only through the annular nozzle at necking 30.
  • An aspirating influence is induced at the venturi structure 28 from a blower 36 that is connected, as indicated at 38, to draw from the interior of kier 10 and to deliver through a heat exchanger at 40 and throttle valve at 42 to the venturi structure at feed connection 34.
  • the short treating liquor is metered into the blower feed to the venturi structure from a mixing tank 44 by a pump 46 connected for delivering formulated treating liquor from tank 44 through an add line 48 having a throttle valve 50 and flow meter 52 installed therein and a nozzle 54 at the downstream end thereof that is fitted to the blower delivery leg 34 so as to discharge therein ahead of (i.e., upstream of) venturi structure 28.
  • the resulting influence at the venturi structure 28 is one of aspiration from the jetted discharge of the blower feed and of distributive application of the metered treating liquor carried by the blower feed.
  • the aspirating influence serves to forward the strand material S through the remainder of the superstructure and also to impose mechanical forces on the strand S by which even distribution of the applied treating liquor is promoted as mentioned earlier.
  • the forwarded strand material S is returned to the kier 10 through the superstructure discharge portion 22 with the flow of air (or other inert gas) resulting from the jetted blower feed and with the applied treating liquor carried in the material.
  • a baffle member 56 is disposed adjacent the returning end of superstructure discharge portion 22 for deflecting the circulating strand S and thereby imposing further incidental mechanical forces in aid of treating liquor distribution as well as directing orderly transient accumulation of the returning strand material in the .I-box storage means 16.
  • a typical piece goods dyeing operation carried out according to the present invention in apparatus starts with loading the kier 10 by introducing one end of the piece goods through the loading port 14 and directing it over roll member 26 with the drive thereto running and with blower 36 operating to feed the venturi structure 28 with air, so that the goods are progressively forwarded through the superstructure and returned to the J-box storage means 16 in kier 10 where the leading end will work its way within reach through the loading port.
  • a leader is helpful in expediting this step.
  • the kier 10 should provide a unit load capacity of about 250 pounds.
  • the kier 10 can, of course, be elongated horizontally to accommodate multiple strand handling arrangements of the FIG. 1 sort, and when this is done the load capacity should increase by a corresponding multiple.
  • a polyester/acrylic fabric treated in apparatus generally comparable to that shown in FIG. 1 formed a strand S of approximately 450 yards.
  • the next step is to apply the dyestuff which will already have been formulated in the mixing tank 44.
  • a disperse dye for the polyester and a basic dye for the acrylic were selected to produce a blue/pink heather shade.
  • These dyestuffs were formulated in usual fashion, except that a foaming agent was added as taught by the previously mentioned publication, and the formulation was prepared at a liquor ratio of 122.0.
  • a more generally suitable ratio has been found to be I: 1.5. Shorter ratios can be employed, but even distribution becomes difficult if the ratio is made too short. Longer ratios can also be used when desired, although if a ratio of about 1:25 is exceeded liquor is apt to exist outside the substrate and this condition should be avoided unless particular circumstances require it.
  • the apparatus should be arranged to circulate the strand S at about 300 yards per minute and the dyestuff formulation should be metered into the air stream ahead of the venturi structure 28 so that it has been added in about minutes.
  • the add rate was 4.5 gallons per minute, which was set by the throttle valve 50.
  • circulation of the strand S is continued for a comparable period (i.e., about 15 minutes) to obtain thorough distribution, while temperature within the kier 10 is maintained below that at which the dyestuff becomes substantive (e.g., usually below about 100F.) throughout this initial portion of the processing.
  • the heat exchanger 40 is operated to supply whatever cooling effect is needed to counteract heating of the air feed to venturi structure 28 by blower 36.
  • the dyestuff Upon application and distribution of the dyestuff in the foregoing manner, the dyestuff is caused to strike by elevating the kier temperature with the loading port 14 closed so as to pressurize the kier and aid in suppressing moisture loss.
  • the heat exchanger 40 is used for this purpose, together with a supplementary heating means 58 arranged within kier l0 and a steam line 60 through which steam is fed to kier 10 to maintain an even moisture level in the strand S during the temperature elevation.
  • a fixing temperature of 250F. was needed, and was reached in 30 minutes, after which circulation was continued for a like period at this temperature.
  • FIG. 1 indicates an arrangement for impressing suction at roll member 26 through a line 62 running to a vacuum pump 64 that exhausts 6 externally of the system.
  • suction type rolls are characterized by a perforate working surface
  • line 62 is arranged to draw at the interior of a suction type roll member 26 extraction of the strand S trained thereover will result, and the extract will be dumped by the externally exhausting vacuum pump 64.
  • the heat exchanger 40 should first be operated to bring the kier temperature below the boiling point of water (e.g., to about 180F.) so that kier 10 can be openedto the atmosphere at loading port 14 during the extraction. With the strand 5 still circulating, the vacuum pump 64 is placed in full operation to extract foam and moisture. The extraction should be continued during at least two complete circulations of the strand S. Then a water rinse may be applied using the same facilities provided for the dyestuff application and at the same liquor ratio (about 1:15). About four circulations of the strand S should be allowed for the rinse water application, after which a second extraction and rinse followed by a final extraction will place the goods in excellent condition for unloading and subsequent handling. Total processing time of 2 to 2 /zhours, including such extraction and rinsing, is normal.
  • FIG. 2 diagrams an alternate arrangement for impressing suction at the roll member 26 through a vacuum line 66 running through a water separator 68 to the suction leg 38 for blower 36 beyond a throttle valve 70 which may be adjusted to obtain the level of suction desired in vacuum line 66.
  • the separator 68 is provided with a drain at 72 for dumping the extract.
  • Both the FIG. 1 and FIG. 2 arrangements additionally include a water line 74 to kier l0 and a kier drain at 76 for general utility purposes.
  • a water line 74 to kier l0 and a kier drain at 76 for general utility purposes.
  • the kier drain 76 is shown as being connected to kier 10in common with the suction leg 38 of blower 36, but that in practice some provision (not shown) would be needed to prevent any liquid collecting at the bottom of kier 10 during blower operation, such as condensate, from being drawn into the blower suction leg.
  • it will be easiest to make such provision by connecting the blower suction leg 38 separately at a level above that of any likely or intended liquid accumulation in kier 10 during blower operation.
  • FIGS. 3 through 9 of the drawings represents, as mentioned earlier, an equipment design incorporating certain modifications developed in adapting the invention fully to the practical considerations of production use.
  • these modifications are concerned with the superstructure arrangement provided for effecting circulation of the strand material to be treated, and with an improved extraction means included in the modified superstructure arrangement.
  • the modified apparatus embodiment illustrated will be seen again to comprise a cylindrical pressure vessel or kier mounted to stand on a base 102 with its axis disposed horizontally to form a treating chamber.
  • the kier 100 is provided with a loading port at 104 and with internally spaced J-box partitioning, as indicated in dotted lines at 106 and 108, to form a storage or accumulation space for the greater portion of the strand material being treated, although it should be noted that in this instance the J-box partitioning 106 and 108 has a special configuration for relating it to the modified superstructure arrangement and that the superstructure arrangement provides an additional loading port as will be pointed out further presently.
  • the kier 100 is fitted with an inspection and access port 110 (see FIG. 4) through which the kier interior can be viewed during processing operation and at which the kier can be opened to the atmosphere whenever desired or access to the interior can be gained whenever necessary.
  • the intake and discharge legs 112 and 114 have a lengthwise tubular conduit form proportioned in cross section for circulation of strand material freely therethrough, and the intake leg 112 into which the circulating strand material is lifted from kier 100 is mounted at a flanged kier outlet 118 arranged adjacent the loading port 104 and aligned vertically above the exit end of the J-box configuration formed by the interior kier partitioning 106 and 108 which terminates in vertical portions at 106 and 108 for such alignment.
  • Both of these flat sections 106" and 108" are inclined in tangent relation to the continuing arcuate form of the J-box partitioning and extend to the inner kier wall face so as to form an entrance portion that is closed except for restricted perforations (not shown) adjacent the upper end of inner flat section 106" that serve to release the aspirating gas discharge sufficiently to avoid an undue pressure buildup in the entrance portion while maintaining a static pressure thereat which materially assists in movement of the accumulated strand material through the J-box space.
  • the horizontal terminal portion 120' of inlet fitting 120 has the related significance of causing the aspirating gas discharge to project the returning strand material against a facing area of the outer J-box partitioning 108 from which it then falls away in a varying pattern toward the lower end portion of inner flat section 106" to be directed therefrom into the continuing J-box space for accumulation.
  • the returning strand material is immediately subjected to substantial and repeated impact forces serving importantly to promote effective treating liquor foam generation and distribution.
  • the initial projection of the strand material into the J-box space in the foregoing manner produces an orderly piling of the strand material therein that facilitates its movement therethrough and particularly eases its lifting from the exit end into the superstructure at which circulation is effected.
  • This additional loading port is provided because the venturi-jet, at which the aspirating influence for strand material circulation and treating liquor application is produced, is installed in the superstructure discharge leg 1 14 so that capability for loading strand material at housing 1 16, or of introducing a loading leader thereat, substantially facilitates the loading step.
  • a slotted sector bracket 152 is suitably provided for fixing the lever structure 144 at a given setting by means of a clamp screw at 144', and, if desired, this sector bracket 152 may bear suitable indicia for indicating the size of venturi orifice provided at a given lever structure setting.
  • the remaining intake leg component 112 of the modified superstructure incorporates the improved extraction means mentioned earlier, as illustrated in FIG. 5.
  • the intake leg 112 includes a concentric housing member 160 enclosing an annular space that is divided into upper and lower chamber portions by a medially fixed annular partition 162, with a lateral inlet fitting 164 opening into the upper chamber and a lateral outlet fitting 166 opening from the lower chamber.
  • a coaxially mounted intake tube 168 having its upstream end flared as shown, is extended from the lower end of intake leg 112 into the lower chamber short of the medial partition 162, and a similarly mounted delivery tube of corresponding diameter is disposed within the upper chamber above medial partition 162.
  • This arrangement is operated for extraction purposes at the conclusion of a wet processing treatment by pressure feeding an inert gas, normally air, to the upper housing chamber so that an inwardly and oppositely directed jet action is applied to the strand material which its circulation is maintained by the venturi-jet in superstructure discharge leg 114.
  • an inert gas normally air
  • the result is a displacement of moisture in the strand material through strand material penetration by the jet directed gas that generates a gas suspended extract continually as the strand material circulates.
  • the penetrating action of the jet directed gas tends to increase with increasing jet opposition to strand material circulation, but such increase is accompanied by an increase in tension on the circulating strand material which is generally undesirable. Accordingly, an angle of jet incidence should be employed that avoids subjecting the strand material to undue tension under given processing conditions.
  • the heat exchanger 184 is provided to control the air (or gas) delivery temperature at a suitable level until temperature elevation is needed for dye fixing or the like, and for this purpose is arranged with water supply and drain lines 186 and 188 under the control of a cooling signal system at 190 that responds to suitable temperature sensing means (not illustrated) to monitor the heat exchanger throughput for whatever cooling effect is needed.
  • a kier drain system at 210 is additionally arranged to serve the blower 178 and to allow recycling from either kier 100 or blower 178 to pump 192 through connections at 212 and 214 whenever liquor collecting at the kier bottom or in the blower for any reason contains enough treating liquor to make recycling desirable.
  • a steam supply line for kier 100 is provided at 216 (compare FIG. 3 with FIG. 9) for use in elevating temperature and maintaining strand moisture content during dye fixing, an air pad supply line at 218 is also preferably provided for use in pressurizing kier 100 to a desired level prior to temperature elevation.
  • the steam supply line 216 is alternatively used for connecting hot or cold water fill lines 220 and 222 with kier 100.
  • the second alternative avoids the water separation burden and can be preferable as the simpler one if the lesser extraction results obtained are sufficient for the particular conditions at hand.
  • the discharge line 228 still functions effectively to carry off the gas-suspended extract by reason of the fact that the feed from auxiliary blower 224 then becomes an external one that results in increasing kier pressure enough to leave discharge line 228 and dump outlet 232 as the easiest path for escape of the gas-suspended extract.
  • the kier 100 is fitted with vent and relief valves, as indicated in FIG. 9 at 234 and 236, in the usual manner and for the usual purposes, and the operating system illustrated in FIG. 9 is well suited for automatic monitoring from suitably located sensors employed to trigger operation of the system components in appropriate sequence and timed duration.
  • this moist condition of the kier atmosphere significantly improves the effectiveness with which heat energy is transferred from the blower to the material being processed and accounts in large mea sure for the rapid rates at which temperature can be elevated according to the present invention in reliance on blower heat input together with steam injection.
  • Apparatus adapted for wet processing textile strand material with a treating liquor formulated for effective application at a short liquor ratio, said apparatus comprising a pressure kier, means for circulating said strand material in traveling strand form to and from a pleated accumulation within said kier, said circulating means including a venturi-jet through which said strand material is trained for circulation and a closed system for supplying an inert gas to said jet under pressure so as to generate an aspirating influence thereat for inducing strand material circulation, and means for applying said treating liquor formulation from a source outside said kier by metering the formulation into the inert gas supply ahead of the venturi-jet during circulation of said strand material.
  • said circulating means additionally includes a lifter roll over which said strand material is trained adjacently ahead of said jet.
  • heating means is disposed within said kier, and said kier is fitted with a connection for supplying steam therein.

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  • Engineering & Computer Science (AREA)
  • Textile Engineering (AREA)
  • Treatment Of Fiber Materials (AREA)
US381268A 1972-12-26 1973-07-20 Apparatus for wet processing of textile materials Expired - Lifetime US3921420A (en)

Priority Applications (13)

Application Number Priority Date Filing Date Title
US381268A US3921420A (en) 1972-12-26 1973-07-20 Apparatus for wet processing of textile materials
CA186,980A CA1007009A (en) 1972-12-26 1973-11-29 Wet processing method and means
GB5562973A GB1430279A (en) 1972-12-26 1973-11-30 Wet processing method and apparatus
CH1698473D CH1698473A4 (es) 1972-12-26 1973-12-04
CH1698473A CH593374B5 (es) 1972-12-26 1973-12-04
DE2360436A DE2360436A1 (de) 1972-12-26 1973-12-04 Verfahren und vorrichtung zur nassbehandlung von textilem strangmaterial
IT1740/73A IT1005527B (it) 1972-12-26 1973-12-11 Metodo ed apparecchiatura per trattamento ad umido
DD175441*A DD107605A5 (es) 1972-12-26 1973-12-18
FR7345466A FR2214248A5 (es) 1972-12-26 1973-12-19
JP49004587A JPS4994979A (es) 1972-12-26 1973-12-24
ES421783A ES421783A1 (es) 1972-12-26 1973-12-26 Procedimiento y aparato para el tratamiento en humedo de genero textil fibroso.
NL7317743A NL7317743A (es) 1972-12-26 1973-12-27
US05/616,152 US4001945A (en) 1973-07-20 1975-09-24 Wet processing means

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US31808772A 1972-12-26 1972-12-26
US381268A US3921420A (en) 1972-12-26 1973-07-20 Apparatus for wet processing of textile materials

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
US31808772A Continuation-In-Part 1972-12-26 1972-12-26

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US05/616,152 Division US4001945A (en) 1973-07-20 1975-09-24 Wet processing means

Publications (1)

Publication Number Publication Date
US3921420A true US3921420A (en) 1975-11-25

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US381268A Expired - Lifetime US3921420A (en) 1972-12-26 1973-07-20 Apparatus for wet processing of textile materials

Country Status (11)

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US (1) US3921420A (es)
JP (1) JPS4994979A (es)
CA (1) CA1007009A (es)
CH (2) CH593374B5 (es)
DD (1) DD107605A5 (es)
DE (1) DE2360436A1 (es)
ES (1) ES421783A1 (es)
FR (1) FR2214248A5 (es)
GB (1) GB1430279A (es)
IT (1) IT1005527B (es)
NL (1) NL7317743A (es)

Cited By (29)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4020658A (en) * 1974-05-04 1977-05-03 Thies Alfred Jun Apparatus for wet-treating fabrics
US4036038A (en) * 1976-05-20 1977-07-19 Gaston County Dyeing Machine Company Apparatus for low liquor ratio wet processing of textile fabric
US4114407A (en) * 1976-05-27 1978-09-19 Gaston County Dyeing Machine Company Soft flow jet dyeing machine
US4129017A (en) * 1977-01-27 1978-12-12 Burlington Industries, Inc. Lab sample jet dyeing machine
US4198204A (en) * 1976-11-27 1980-04-15 Hoechst Aktiengesellschaft Short liquor dyeing process for piece goods, made from cellulose fibers, in rope form
US4351076A (en) * 1979-02-17 1982-09-28 Hoechst Aktiengesellschaft Process for the treatment of textiles in jet dyeing apparatuses
EP0078022A1 (de) * 1981-10-24 1983-05-04 Hoechst Aktiengesellschaft Verfahren zum Behandeln von Textilgut in Jet-Färbeanlagen
US4445346A (en) * 1983-02-07 1984-05-01 Keiltex Corporation Apparatus for wet processing textile material in endless rope form
FR2536769A1 (fr) * 1982-11-29 1984-06-01 Air Liquide Procede de neutralisation acceleree de substrats textiles cellulosiques et appareils de mise en oeuvre
US4468937A (en) * 1981-01-23 1984-09-04 Attilio Bertoldi Machine for the fulling and washing of cord fabrics
WO1985000187A1 (en) * 1983-06-27 1985-01-17 Gaston County Dyeing Machine Company Apparatus for wet treatment of cloth in endless rope form
US4550579A (en) * 1984-04-13 1985-11-05 Frank Clifford G Apparatus for the dyeing of shaped articles
DE3430615A1 (de) * 1984-08-20 1986-02-27 Thies GmbH & Co, 4420 Coesfeld Treibduese fuer die nassbehandlung von textilgut
EP0300359A2 (de) * 1987-07-21 1989-01-25 Hoechst Aktiengesellschaft Verfahren und Vorrichtung zum Behandeln von Textilgut in Jet-Färbemaschinen
EP0310013A1 (de) * 1987-10-01 1989-04-05 Hoechst Aktiengesellschaft Verfahren und Vorrichtung zum Färben von strangförmigem Textilgut
US4829620A (en) * 1983-06-30 1989-05-16 Hoechst Aktiengesellschaft Process for drying textile material in rope form
US4862545A (en) * 1987-07-21 1989-09-05 Hoechst Aktiengesellschaft Method for the removal of fabric samples from HT jet dyeing machines without loss of liquor
US5014526A (en) * 1990-09-21 1991-05-14 Gaston County Dyeing Machine Co. Textile wet processing machine having fabric circulation chamber with adjustable inner wall
US5129242A (en) * 1990-06-18 1992-07-14 Gaston County Dyeing Machine Co. Low-liquid jet machine for wet processing textile fabric
US5170523A (en) * 1990-07-24 1992-12-15 Scholl America, Inc. Method and apparatus for wet processing of fabric
US5577282A (en) * 1995-05-22 1996-11-26 Gaston County Dyeing Machine Company Textile wet processing machine and method
US5873270A (en) * 1997-01-31 1999-02-23 Scholl America, Inc. Textile wet processing machine having an adjustable inner wall
US5987934A (en) * 1997-01-31 1999-11-23 Scholl America, Inc. Textile wet processing machine having an adjustable inner wall
WO2003060223A1 (en) * 2002-01-10 2003-07-24 Milliken & Company Apparatus for batch dyeing
US6676710B2 (en) 2000-10-18 2004-01-13 North Carolina State University Process for treating textile substrates
CN1306097C (zh) * 2003-10-21 2007-03-21 特恩机械（英属维尔京群岛）有限公司 将处理剂均匀涂覆在绳状织物上的方法和设备
EP2559798A1 (en) * 2011-05-11 2013-02-20 Zhejiang Yinhe Printing & Dyeing Co., Ltd Airflow atomization dyeing machine system and water-utilization method therefor
WO2016180389A1 (de) * 2015-05-08 2016-11-17 Thies Gmbh & Co. Kg Vorrichtung zum kontinuierlichen entwässern einer textilen warenbahn
CN112161457A (zh) * 2020-09-30 2021-01-01 彭德敏 一种印染用旋转收折烘干布料装置

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DE2718941A1 (de) * 1976-05-07 1977-11-17 Sandoz Ag Verfahren zum einbadigen waschen und faerben von textilen flaechengebilden in haspelkufen oder faerbetrommeln
DE2623315C3 (de) * 1976-05-25 1981-04-02 Brückner-Apparatebau GmbH, 6120 Erbach Verfahren zur Naßbehandlung von Textilgut sowie Haspelkufe zur Durchführung des Verfahrens
GB8301018D0 (en) * 1983-01-12 1983-02-16 Lyles Sons & Co Ltd S Apparatus for treatment of yarns & c
NL8502947A (nl) * 1985-07-16 1987-02-16 Flexline Services Ltd Werkwijze en inrichting voor het impregneren van uit verschillende filamenten bestaande draden, linten of dergelijke die eventueel in een weefsel of breisel, e.d. verwerkt zijn.

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Cited By (45)

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US4020658A (en) * 1974-05-04 1977-05-03 Thies Alfred Jun Apparatus for wet-treating fabrics
US4036038A (en) * 1976-05-20 1977-07-19 Gaston County Dyeing Machine Company Apparatus for low liquor ratio wet processing of textile fabric
US4114407A (en) * 1976-05-27 1978-09-19 Gaston County Dyeing Machine Company Soft flow jet dyeing machine
US4198204A (en) * 1976-11-27 1980-04-15 Hoechst Aktiengesellschaft Short liquor dyeing process for piece goods, made from cellulose fibers, in rope form
US4129017A (en) * 1977-01-27 1978-12-12 Burlington Industries, Inc. Lab sample jet dyeing machine
US4351076A (en) * 1979-02-17 1982-09-28 Hoechst Aktiengesellschaft Process for the treatment of textiles in jet dyeing apparatuses
US4468937A (en) * 1981-01-23 1984-09-04 Attilio Bertoldi Machine for the fulling and washing of cord fabrics
US4483032A (en) * 1981-10-24 1984-11-20 Hoechst Aktiengesellschaft Process for treating textile material in jet dyeing machines
EP0078022A1 (de) * 1981-10-24 1983-05-04 Hoechst Aktiengesellschaft Verfahren zum Behandeln von Textilgut in Jet-Färbeanlagen
FR2536769A1 (fr) * 1982-11-29 1984-06-01 Air Liquide Procede de neutralisation acceleree de substrats textiles cellulosiques et appareils de mise en oeuvre
EP0112744A2 (fr) * 1982-11-29 1984-07-04 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Procédé de neutralisation accélerée de substrats textiles cellulosiques et appareils de mise en oeuvre
EP0112744A3 (en) * 1982-11-29 1984-10-24 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Process for the accelerated neutralisation of cellulosic textile materials, and apparatus therefor
US4536907A (en) * 1982-11-29 1985-08-27 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Process for effecting an accelerated neutralization of cellulose textile substrates impregnated with alkaline hydroxide
US4445346A (en) * 1983-02-07 1984-05-01 Keiltex Corporation Apparatus for wet processing textile material in endless rope form
US4716744A (en) * 1983-06-27 1988-01-05 Gaston County Dyeing Machine Company Apparatus for wet treatment of cloth in endless rope form
WO1985000187A1 (en) * 1983-06-27 1985-01-17 Gaston County Dyeing Machine Company Apparatus for wet treatment of cloth in endless rope form
US4829620A (en) * 1983-06-30 1989-05-16 Hoechst Aktiengesellschaft Process for drying textile material in rope form
US4903509A (en) * 1983-06-30 1990-02-27 Hoechst Aktiengesellschaft Apparatus for drying textile material in rope form
US4550579A (en) * 1984-04-13 1985-11-05 Frank Clifford G Apparatus for the dyeing of shaped articles
DE3430615A1 (de) * 1984-08-20 1986-02-27 Thies GmbH & Co, 4420 Coesfeld Treibduese fuer die nassbehandlung von textilgut
US4862546A (en) * 1987-07-21 1989-09-05 Hoechst Aktiengesellschaft Process of treating textile material in jet dyeing machines and apparatus for performing same
US4862545A (en) * 1987-07-21 1989-09-05 Hoechst Aktiengesellschaft Method for the removal of fabric samples from HT jet dyeing machines without loss of liquor
EP0300359A2 (de) * 1987-07-21 1989-01-25 Hoechst Aktiengesellschaft Verfahren und Vorrichtung zum Behandeln von Textilgut in Jet-Färbemaschinen
EP0300359A3 (en) * 1987-07-21 1989-06-21 Hoechst Aktiengesellschaft Method and apparatus for treating textile materials in jet machines
EP0310013A1 (de) * 1987-10-01 1989-04-05 Hoechst Aktiengesellschaft Verfahren und Vorrichtung zum Färben von strangförmigem Textilgut
US4885814A (en) * 1987-10-01 1989-12-12 Hoechst Aktiengesellschaft Process for continuous treatment, preferably dyeing, of textile material in rope form
US4947660A (en) * 1987-10-01 1990-08-14 Hoechst Aktiengesellschaft Apparatus for continuous treatment, preferably dyeing, of textile material in rope form
US5129242A (en) * 1990-06-18 1992-07-14 Gaston County Dyeing Machine Co. Low-liquid jet machine for wet processing textile fabric
US5170523A (en) * 1990-07-24 1992-12-15 Scholl America, Inc. Method and apparatus for wet processing of fabric
US5014526A (en) * 1990-09-21 1991-05-14 Gaston County Dyeing Machine Co. Textile wet processing machine having fabric circulation chamber with adjustable inner wall
US5577282A (en) * 1995-05-22 1996-11-26 Gaston County Dyeing Machine Company Textile wet processing machine and method
US5873270A (en) * 1997-01-31 1999-02-23 Scholl America, Inc. Textile wet processing machine having an adjustable inner wall
US5987934A (en) * 1997-01-31 1999-11-23 Scholl America, Inc. Textile wet processing machine having an adjustable inner wall
US6676710B2 (en) 2000-10-18 2004-01-13 North Carolina State University Process for treating textile substrates
WO2003060223A1 (en) * 2002-01-10 2003-07-24 Milliken & Company Apparatus for batch dyeing
US6672114B2 (en) * 2002-01-10 2004-01-06 Milliken & Company Apparatus for batch dyeing
CN1306097C (zh) * 2003-10-21 2007-03-21 特恩机械（英属维尔京群岛）有限公司 将处理剂均匀涂覆在绳状织物上的方法和设备
EP2559798A1 (en) * 2011-05-11 2013-02-20 Zhejiang Yinhe Printing & Dyeing Co., Ltd Airflow atomization dyeing machine system and water-utilization method therefor
EP2559798A4 (en) * 2011-05-11 2014-01-22 Zhejiang Yinhe Printing & Dyeing Co Ltd AIR FLOW DUSTING AND STAINING MACHINE, AND SYSTEM AND WATER UTILIZATION METHOD THEREFOR
WO2016180389A1 (de) * 2015-05-08 2016-11-17 Thies Gmbh & Co. Kg Vorrichtung zum kontinuierlichen entwässern einer textilen warenbahn
WO2016180390A1 (de) * 2015-05-08 2016-11-17 Thies Gmbh & Co. Kg Verfahren zur behandlung eines textilen substrates sowie vorrichtungen zur durchführung des verfahrens
CN107636221A (zh) * 2015-05-08 2018-01-26 蒂斯有限及两合公司 用于处理纺织基材的方法以及用于执行该方法的装置
CN107636221B (zh) * 2015-05-08 2020-08-21 蒂斯有限及两合公司 用于处理纺织基材的方法以及用于执行该方法的装置
US10895031B2 (en) 2015-05-08 2021-01-19 Thies Gmbh & Co. Kg Method for the treatment of a textile substrate, and devices for carrying out said method
CN112161457A (zh) * 2020-09-30 2021-01-01 彭德敏 一种印染用旋转收折烘干布料装置

Also Published As

Publication number Publication date
IT1005527B (it) 1976-09-30
GB1430279A (en) 1976-03-31
JPS4994979A (es) 1974-09-09
CH1698473A4 (es) 1977-02-15
DE2360436A1 (de) 1974-06-27
CH593374B5 (es) 1977-11-30
NL7317743A (es) 1974-06-28
ES421783A1 (es) 1976-07-16
CA1007009A (en) 1977-03-22
DD107605A5 (es) 1974-08-12
FR2214248A5 (es) 1974-08-09

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