US3504999A - Process for dyeing textile fiber materials - Google Patents

Description

April 7, 1970 Y' l.. DRAGO 3,504,999

PROCESS FOR DYEING TEXTILE FIBER MATERIALS original Filed oct. 4. 1965 2 sheets-sheet x 34 36 /6 /E. 1 a x INVENTOR LEO D GO BYMLM ATTORNEY:

April v7, 1970 L. DRAGO 3,504,999

PaocEss Foa DTETNG TEXTILE FIBER MATERIALS original Filed oct. 4, 1965 2 sheets-sheet 2 INVENTOR LEO DRAGO ATTORNEYpr United States Patent Int. c1. Dosp 3/14 U.S. Cl. 8--54 6 Claims ABSTRACT OF THE DISCLOSURE A process for pad-dyeing of slubbing or tow is provided wherein the slubbing in saturated with a padding liquor which is then prefixed on the fibers by thermal treatment thereof with saturated steam while the slubbing is squeezed in a downward moving path and in a loose state. The prefixed material is deflected from its downward path into a generally horizontal path While it is simultaneously formed into uniform vertical folds. Thereafter the prefixed and folded material is subjected to a second thermal treatment with steam.

This application is a divisional application of my application Ser. No. 492,725, led Oct. 4, 1965, now U.S. Patent No. 3,326,022 which in turn is a continuation-impart of my abandoned application Ser. No. 338,381, filed Jan. 17, 1964.

The present invention relates to an apparatus and process for the continuous wet-treatment and especially the dyeing of textile fiber materials such as wool and similar fibers with a dye liquor.

More particularly, the invention relates to the continuous dyeing of polyamide and acrylic fiber materials in the form of slubbings (or tops).

By the expression, slubbings (or tops) there is meant any product known in the spinning and weaving art as slubbings or tops, card slivers, spun ribbons, or the like. This expression also comprises tow. Wherever slubbing is treated according to the process and in the apparatus of this invention, tow can be treated equally in lieu of slubbing.

The concept of dyeing wool and other textile fibers, especially in theform of slubbing and the like, in a continuous process is not new. Many and varied suggestions have been made as to Ways in which this may be accomplished. There is, for example, the method of using neutral or acid steam for fixing the dyestuff after the latter has been deposited on the wool. The use of an atmosphere of steam for fixing a dyestuf has also been known for a long time in the textile printing art. However, with the exception of the vigoureux process, this method of after-treatment with steam has not, up to quite recently, been found to be economical in the case of wool and the like textile fiber materials because the resulting dyed goods usually present a skittery, i.e., unevenly dyed aspect. On wool, a prerequisite of successful dyestufi fixation with steam is that the steam is saturated but not superheated. There are in existence machines with which woollen piece goods, but no slubbings, can be dyed by this process.

There are also other machines for the dyeing of wool slubbing which consist mainly of a large container in the form of a horizontally disposed cylinder which is provided at one end with a socket for admittingthe dyed but still unfixed slubbings and at the other end with a dis- 3,504,999 Patented Apr. 7, 1970 charge pipe for the steam-fixed dyed slubbings. In the opening of the feed socket, there is often housed a pad mangle which closes this socket against the escape of steam while feeding the slubbing therethrough into the interior of the cylinder. The outlet pipe is provided with a series of rollers which, at the same time, close the pipe against the escape of steam while effecting withdrawal of the slubbing from the cylinder. In the interior of the cylinder, there is provided a conveyor belt for moving the slubbing, fed onto the same through the entry socket, toward the outlet pipe. Slubbings are placed by means of a cutling frame or other conventional means on one end of the conveyor belt, while from the other end of the conveyor belt, the steamed slubbing is withdrawn through the aforesaid series of rollers in the outlet pipe.

Steam is continuously fed into the cylinder in an attempt to maintain in the latter the atmosphere most favorable for fixing as explained hereinbefore, namely saturated steam, while the cylinder is being heated simultaneously to operational temperature.

However, it is very difiicult to control the rate of steam and the temperature sufiiciently exactly to maintain the desired optimal atmosphere. Instead, the steam atmosphere in the cylinder is frequently either superheated or moist, resulting either in skittery or insufficiently fixed dyeings of wool slubbings.

Many of the above-mentioned difficulties have been overcome in a known, more recent apparatus for fixing on slubbings, e.g. of wool, the dyestuf which has been applied thereto from a dye liquor, which apparatus comprises means for contacting the slubbings with steam for heating and simultaneously moistening them, and comprises as a principal element of construction a vertically disposed J-tube open at both ends and being located beneath a padding device, which J-tube comprises:

(a) an upper section serving as a steam room, and

(b) an elongated, tubular lower section of approximately J -shaped longitudinal section, which lower section is freely communicatingly connected with the top end of the J to the bottom of said steam room, and has a smooth inside surface.

The lower portion of the substantially J-shaped longitudinal section extends with the longer straight portion of the .l downwardly from the upper section, the longer straight portion being preferably from about 8 to 12 times as long as the upper section of the J-tube is high, while the shorter portion of the J extends upwardly at an angle from the lowermost zone of the I, which angle is about 30 to 70, depending on the ratio of the length of said lower portion to that of the said longer straight portion.

Finally, this known apparatus comprises means for withdrawing the fixed dyed slubbings from the open exit of the lower section of said I-tube.

The J-tube is provided with a feed opening adapted for admitting the still unfixed dyed slubbings from the padding device exclusively under their own weight into the interior of the J-tube, devices for introducing fresh steam in jet form directly into the upper portion of the .l-tube, into direct contact with the slubbings introduced thereinto, while preventing the steam in jet form from impinging directly on the slubbings andpreventing water particles carried by the steam from coming into contact with the slubbings.

This otherwise highly satisfactory apparatus suEers from the drawback that, in industrial operation, it requires undesirably high structures. The J-tube arrange- -ment alone may attain heights of 12 meters, and, if undesirable length of travel of the impregnated, but still unxed textile material is to be avoided, it is then necessary to provide a padding station at such undesirably high level above the foundation of the dyeing plant.

Another drawback resides in a certain lack of control of the relative conditions prevailing in the upper section serving as steam-room and the subsequent lower section of the I-tube.

It is, therefore, an object of the present invention to provide an apparatus for the continuous dyeing and steaming of pad-dyed slubbing or tow, e.g. of polyamide fibers such as wool or nylon or of acrylic fibers, whereby dyed and fixed slubbings of -unobjectionable quality are obtained, the dyeing being fully fixed and perfectly even over the whole length as well as the entire cross section of each slubbing or tow.

This, and other objects which will become apparent hereinafter, are attained, according to a first aspect of the present invention, by a process which comprises:

(a) saturating a slubbing or the like textile material as defined with at least one bath of padding liquor,

(b) squeezing the material out to remove therefrom liquor exceeding -a limit amount of about 50 to not more than 200% of the weight of the impregnated goods,

(c) subjecting the squeezed material during a downward movement thereof through a first zone A1 in a loose state and free from contact with any supporting and/or conveying means to a first, preliminary thermal treatment with dry steam whereby the treating bath components are prefixed on the fibers of the material to such a degree that no substantial amounts of dye are left capable of migrating along the fibers of the impregnated material.

(d) defiecting the prefixed material gradually from its downward to a substantially horizontal movement preferably while causing the same simultaneously to form uniform folds, and

(e) subjecting the prefixed and preferably folded material during its subsequent horizontal movement through a second zone A2 in which the folds are preferably in vertical position, to a second thermal treatment, preferably with steam, which treatment is separate from the thermal treatment under (c), while substantially no exchange of heating medium takes place between the two zones of treatment in steps (c) and (e).

During the stage (c), the residual pad-liquor on the slubbing spreads throughout the fibrous structure of the latter to attain a uniform distribution thereon and to penetrate to a sufficient degree into the fibers so that at the end of this treatment no further extraction of dye with water or further migration of the liquor along the fibers in significant amounts are possible.

The downward movement of the material through the prefixing first zone A1 should take place at a constant, substantially uniform rate.

On leaving the pre-fixing zone, the prefixed slubbing is deflected gradually by an angle of about 90 and is thus caused to move on in a substantially horizontal direction through the subsequent second fixing zone A2 in which treatment the prefixed dye-liquor penetrates from the outer fiber layers into the core of each fiber, whereby the fixing treatment is completed.

It is very important that, during the deection about an angle of about 90, the slubbing or the like material be laid into folds which retain a substantially vertical arrangement throughout the movement of the material through the second fixing zone A2.

In the following, there are given preferred ranges of conditions to be observed in the prefixing first zone A1 on the one hand and in the second fixing zone A2 on the other hand.

When treating wool slubbing, especially when it is impregnated with metal-complex dyes, travel rates of the slubbing range from 4 to 8 meters per minute and an atmosphere of saturated steam of 98 to 102 C., in the first zone A1 are recommended. For the same material, a treatment period of l5 to 30 minutes and an atmosphere of saturated steam of 102 to 103 C. are recommended in the fixing zone A2. Essentially the same applies to woolen QW,

When treating nylon slubbing, similar conditions are recommended for both fixing zones as in the case of wool, but the temperature especially in the fixing zone A2 may also be somewhat higher.

In the case of acrylic fibers, travel-rates of 5 to 7 meters per minute :and a superheated steam atmosphere of 102 to 107 C. for prefixing zone A1 and a treatment time for each slubbing fold from 15 to 20 minutes and an atmosphere of over-heated steam of 102 to 107 in fixing zone A2 are recommended. Darker shades require a longer presence of the slubbing folds in the fixing zone A2 and, correspondingly, a lower travel rate of the slubbing in the first zone A1.

Excessively low travel-rates in the first zone A1 and excessively long presence of the textile material in the second zone A2 lead to color-losses in the surface layer of the fibers causing an undesirable sandwich effect.

A preferred apparatus for carrying out the process according to this aspect of the invention comprises, in a first type of embodiment, a padding station of known construction consisting of one or more treating baths in combination with squeezing members, and subsequently arranged a novel kind of steaming station comprising at least one vertically disposed prelixing chamber, means for feeding padded and squeezed, but still unfixed slubbing or the like textile material from above into the pre-fixing chamber, heating means associated with the pre-fixing chamber and adapted for introducing heating fiuid into the latter, defiecting duct means in free communication with the lower opening end of the pre-fixing chamber, conveying means arranged above the pre-fixing chamber to facilitate feeding of the slubbing or the like material into the latter chamber along the vertical axis of the said chamber, holding the slubbing substantially equidistant from the walls of said chamber.

The width of the pre-fixing chamber, i.e. the distance of its walls from the material passing therethrough must be sufficient to permit full `blowing of the slubbing in the pre-fixing chamber without causing any frictional contact between slubbing and wall and to permit the formation of well developed folds in the defiecting duct below the pre-fixing chamber.

The curvature of the deliecting duct extends through an angle, measured along the central axis of the duct, which ranges from at least 45 to not more than 90, and preferably through an angle of 60 to 80; the radius of the curved portion of the central duct axis should be at least equal to twice the internal width of the pre-fixing chamber and preferably not exceed about three times that width, taken in the plane of the said curved central axis portion.

The curved deliecting duct opens with its lower discharge end into a second fixing chamber the longitudinal horizontal axis of which is perpendicular to the axis of the pre-fixing chamber.

The length of the pre-fixing chamber ranges from about one eighth to one third of the longitudinal extension of the second fixing chamber D.

Preferably, the portion of the upper reach of the conveyor means which extends from the lower open end of the defiecting duct to the discharge end of the upper reach where the dye-fixed slubbing is taken off the conveyor, is about four to five times as long as the pre-fixing chamber is high.

In another type of embodiment of the apparatus according to the invention two or more pairs of padding stations and steaming stations are arranged in series.

The length of the curved duct portion should be from about the same to not more than twice the height of the pre-fixing chamber. Preferably it should not exceed one and a half times the length of the latter chamber.

The apparatus aspect of the invention is further illustrated in the accompanying drawings in which FIGURES la and 1b taken together represent a longitudinal sectional view through a first embodiment of a steaming station forming part of the apparatus according to the invention;

FIGURE 2 represents an enlarged sectional view along line II-II of a portion of the apparatus section shown in FIGURE 1;

FIGURE 3 is an enlarged detail View 0f the exit region of the apparatus section shown in FIGURE la;

FIGURES 4a and 4b taken together show a longitudinal sectional view of a preferred embodiment of the apparatus according to the invention.

Relating now to the drawings more in detail, and in particular to FIGURES la, lb and 2 thereof, the embodiment shown therein comprises a steaming station consisting essentially of a pre-fixing chamber B and a second or main fixing chamber D.,Above pre-xing chamber B there is arranged a couple of squeezing rollers i. These squeezing rollers pertain to the padding station the remainder of which is not shown in these figures. Squeezing rollers 10 serve to squeeze ol padding liquor from the slubbing A while withdrawing the latter from the impregnation -bath or baths of the padding station and conveying it to the steaming station.

A complete steaming station is illustrated in FIGURES 4a and 4b; special conveying means interposed between the squeezing rollers and the steaming station, as they are shown in FIGURES 4a and 4b, can, of course, also be interposed between squeezing rollers 10 and the entry opening for the slubbing at the top of the steaming station shown in FIGURES 1a and 1b.

Slubbing A coming from the squeezing rollers 10 or from interposed conveying means is introduced into the pre-fixing chamber B through the open top end of the latter.

Pre-lixing chamber B is constituted by a duct of rectangular cross-section and suitable height of about 40 to 100 and preferably about 60 to 80 centimeters. The walls of duct 14 are provided throughout the entire length thereof with perforations or holes 16. Duct 14 is vertically disposed and is free from any guiding or supporting members for the slubbing, so that the latter, on leaving squeezing rollers 10 can freely enter and pass unimpeded through this duct in downward direction without coming into contact with the walls of the duct. Chamber D is preferably of a length of about 200 to 400 centimeters. The chambers B and D are enclosed in a casing 18. Duct 14 is spaced from the wall of the casing so as to provide an interspace of retangular cross-section consituting a charnber C surrounding duct 14 on all four sides. Chamber C is closed at its upper and lower end by walls and thus constitutes a collecting chamber for a heating fluid, preferably steam. Casing 18 is lined with insulating material 22 and bears a dome 24 of semi-circular cross-section vaulted above the open top end of duct 14, which dome is provided with a rectangular opening 26 through which slubbing A is introduced into pre-fixing chamber B. This opening is provided with inwardly inclined plates 30 which form an entry slot 28. The width of the latter can be varied by means of an adjustable strip or strips 32 which is or are slidably mounted onto one or both of inclined plates 30. Thereby, the width of slot 28 can be adjusted to slubbings A of diiferent thicknesses and forms a satisfactory closure for chamber B, whereby excessive loss of steam or the like heating fluid from that chamber to the outside can be avoided.

A preferably horizontally disposed duct 34 is provided in the peripheral wall of casing 18 about chamber C in the central the iirst zone of that chamber. The inner Wall of this duct separating it from chamber C is provided with a number of apertures 36 establishing communication between chamber C and duct 34. Furthermore, duct 34 is connected by means of connector-socket 38 to a source of heating lluid, especially saturated steam. The provision of the intermediate chamber C between duct 34 and prexing chamber B prevents direct impingement of a steamjet from duct 34 onto the slubbing in zone A1. To the lower open end of duct 14 there is attached a curved deflecting duct 40, the upper open end of which is of the same cross-section as duct 14, while the lower open end 0r discharge opening 42 of this duct 40 is closed by a llap 43 hingedly mounted at the upper rim of opening 42.

The length of this duct 40 is preferably about equal or slightly longer than that .of duct 14.

In the embodiment of FIGURES la, 1b and 2, the curvature of duct 40` extends through an angle of about 65, measured along the central curved axis 40a of duct 40. Discharge opening 42 leads to the interior of xing chamber D in which the final thermal treatment of the slubbing A takes place. This chamber constitutes the second zone A2. An endless conveyor -44- which consists of bars secured to two or more endless chains operated by transmission gears 46 is so mounted in chamber D that it passes with ,its upper reach directly beneath the lower rim `of opening 42; the upper reach of the conveyor is adapted to Imove lirst in horizontal direction and then in slightly ascending direction toward the discharge means in front wall 82 of chamber D.

Conveyor 44 extends within chamber D in a substantially horizontal direction, perpendicular to the axis of duct 14, between sidewalls 47 and is adapted to carry slubbing A. The ascending portion of the upper reach of conveyor 44 is designated by reference numeral 45 and ends adjacent a conveying roller 48 which is flush with an outlet 65. A couple of driving drums 50 are disposed externally of chamber D and serve to pull the completely fixed slubbing =out of the steaming section. Drive means (not shown) are provided to operate these drum means 50 in unison with squeezing rollers 10. Conveyor gear 49 serves as drive gear and is driven from a motor equipped with a speed control device.

Between rollers 48 and 50, at the ,outlet 65, there is arranged a hydraulic closing device F which acts also as a washing means for the slubbing and which provides a casing S2 (see FIGURE 3) subdivided internally thereof into partitions by tubular separating means 54, 56, 518 secured to its side walls to also constitute conveying and guiding members for the slubbing. Separating means 56 and 58 are combined with counter members 57 and 59 respectively.

At the front part of casing 52 above member 54 there is provided a tube 60 which is connected through a connector `62, with a reservoir containing a suitable liquid, eg. water: such tube is provided along its generating line with holes 64 venting to a small basin 66 wherein said tube is disposed.

The edge of one of the longitudinal walls of basin 66 is suitably shaped to form a weir 68 and such edge connects through a wall 70 with the periphery of member 57.

Separating means 56 and 518 form together with the bottom wall of casing 52 a first basin 72 which communicates via separating member 56 acting as a weir, with an adjacent small basin 74 provided with an overow 76 connected to a drain pipe 78.

Hydraulic closing device F is provided as a separate member which is detachably secured in the outlet opening 65 of chamber D. -For this purpose, it casing 52 has flanges whereby it is fastened, for example by means of screws, to the front wall 82 of chamber D.

Upon the bottom of chamber D and underneath conveyor 44 there is arranged a pipe coil 84 fed with steam through connector 85. On the bottom of chamber D there is also provided an overflow 86 connected with a drain pipe 88 whereby a liquid level can be maintained in the chamber to form a sump e.g. of water which covers pipe coil 84 if desired. In the present case over-flow 86 is also a continuation of drain pipe 7-8. Closable drainage means 87 permit emptying of the water sump and introduction of direct steam.

At its upper part chamber D has screens 90 extending towards the duct 40` to form together with the upper walls of said chamber an interspace to avoid dripping of condensed liquid which may form on said walls onto the slubbing on conveyor 44. The side walls of chamber D are provided with inspection doors 92 to check and control the operations carried out on the slubbing in the second zone A2.

In the embodiment of FIGURES 4a and 4b there is shown a complete pad dyeing apparatus comprising a padding station of known construction, a somewhat modified steaming station according to the invention and a subsequent washing station. In this figure like reference numerals designate like parts as in the embodiments of FIG- URES la, 1b and 2; however, several parts have been shown more schematically in FIGURES 4a and 4b.

Structural differences in the embodiment of the steaming station of FIGURES 4a and 4b are the following:

In this embodiment, the duct 14 of the pre-fixing chamber B has no heating jacket, it is provided with two inlets 33 and 35 fitted with valves 33a and 35a respectively, for the direct introduction of steam into the duct 14. Baffie plates 37 placed over each steam inlet prevent jets of steam or of hot water from impinging directly on the slubbing in zone A1. Since there is always a possibility, in spite of the lining of insulating material 22, of condensation occurring in the duct room k14 or of water entering the same via steam inlets 33 and 35, an annular condensate collecting groove 25 equipped with a drain tube 27 is provided at the lower rim of the dome 24, about the inlet opening 26, to gather any condensate that is deposited on the inner wall of the dome.

Furthermore, the hydraulic closing device is replaced by large conveying roll 51 which serves to convey the completely fixed slubbing to the driving drums 50 past a flexible shield 61 mounted by a hinge 63 at the upper rim of exit opening 65. Together, conveying roller 51 and flexible shield 61 cooperate to maintain the exit opening 65 sufficiently closed during the operation to prevent undue loss of steam from fixing chamber D.

In FIGURES 4a and 4b, the padding station comprises not only squeezing rollers shown in FIGURES la and lb, but also a reservoir 11 =for pad-liquor and feeding de* vice 11a through which pad liquor is released to the top side .of the pair of squeezing rollers 10, as well as -guide rollers 13 and a large conveying roller 12 which is located above the inlet opening 26 in the dome 24 closing the pre-fixing chamber B.

In the light of the foregoing, the process according to the invention is performed as follows, or in a similar manner:

At the bottom of chamber D there is provided a certain liquid level determined by the fact whether drain 87 is open or closed, and when the latter is the case, by the position of the overflow 86, while connectors 38 and 85 are fed with steam. Pipe coil 84 is provided with a number of holes 84a through which steam is let into chamber D so as to maintain therein the desired conditions of moisture, if any, and temperature. At the same time, through connector 62 a liquid, preferably water, is led into the small basin 66, which liquid by overflowing along wall 70 of member 57 forms a continuous liquid sheet G ensuring a closure between the interior of chamber D and the outside.

On starting the operation, slubbing A as it emerges from the treating bath, is advanced by squeezing rollers 10 and introduced into chamber B through slot 28.

Slubbing A moves downwardly under the effect of gravity alone at a suitable speed, determined by that of rollers 10, into chamber B without coming into contact with the walls thereof and without having to contact any guiding and conveying member but remaining all the time substantially equidistant from said walls.

Steam is let into chamber C through connector 38 and spreads uniformly throughout said chamber and with the same uniformity passes through holes 16 to act upon both faces of slubbing A. Due to the disposition of holes 16, the thermal action of the steam is effected throughout the entire length and height of chamber B establishing therein determined conditions of treatment (temperature, pressure and humidity) depending on both the nature of the material to be treated and the composition of the treating bath with which slubbing A has been impregnated.

The' free movement of the slubbing in chamber B permits the residual treating liquor impregnating the slubbing to spread uniformly throughout the fibrous structure of the slubbing producing an even distribution of the liquor on the fibers. Slubbing A thus becomes uniformly impregnated with the treating solution, while moving through chamber B at a suitable rate of travel.

Slubbing A in its downward movement leaves pre-fixing chamber B proper and enters the defiecting duct 14.

Due to the specific design of the latter, as the slubbing contacts the curved bottom wall of this duct, it forms superimposed folds extending in planes substantially perpendicular to the direction of travel of the material in chamber B. When a new slubbing first enters with its forward edge this duct 14, the initial somewhat irregular folds come to rest against flap 43 which is then in closed position under its own weight. As fold is superimposed upon fold, the lower portion of the curved duct is gradually filled, the newly formed folds becoming rapidly uniform and extending substantially across the entire crosssection of the duct in this region. As soon as the weight of the column of folds exceeds that of fiap 43, the flap iS pushed open and the folds begin to slide out of the discharge opening 42 onto the moving conveyor belt 44. The free forward edge of the slubbing is inserted into the hydraulic closing device F and between rollers 50. Once the operation has been in progress for a short time, the folds will emerge from discharge opening 42 in substantially upright position and remain therein throughout the horizontal stretch of conveyor 444. As the folds ascend the upwardly inclined stretch of the upper reach of conveyor 44 they begin to tip backward. Consequently, at the upper end of this stretch of the conveyor, the slubbing which is now completely fixed is lifted off the conveyor easily and without any necessity of pulling the web from under a superimposed fold or folds, as would be the case if the folds had been tipped forward instead of backwardly. Forward tipping of the folds which easily occurs if no ascending stretch is provided in the upper reach of the conveyor would lead to frequent tearing of the web.

Flap 43 serves a double purpose, in that, firstly, it prevents development of a chimney-effect in the form of a draft from chamber D through ducts 40 and 14, and, secondly it assists in the beginning of operation with a new slubbing, in the formation of folds of equalized height, i.e. of uniform shape filling well the curved duct 40. While, in FIGURES la and lb, there is shown a stage of fold-formation shortly after flap 43 has opened, FIG- URES 4a and 4b show normal filling of duct 40 with flap 43 fully opened. Through the fact that in the beginning of operation fiap 43 closes opening 42, and that during full operation the folds of the slubbing effectively fill the cross-sectional area of duct 40, steam is prevented from escaping from either one of chambers B and D into the other, and two separate steaming zones with conditions independent in each zone from fluctuations in the other, are maintained in the steaming station at all times.

While the use of flap 43 or a similar mechanical device serving as zone separating means is preferred, the same end can also be achieved to a certain degree by a somewhat narrowed cross-sectional area of the discharge opening 42.

The weight of flap 43 or mechanical equivalents used in its place should not be too low, for it must be sufficient to cause a certain halt in the downward movement of a newly introduced slubbing descending through duct 40; on the other hand, it must not be too high lest the column of folds in the duct build up to such height that it reaches the lower region of chamber B, thus leading to unsatisfactory pre-fixing in that region.

While proceeding through chamber D, the folded slubbing or the two is subjected to the second, final fixing treatment.

Due to the presence of thel steam delivered from pipe coil 84 in chamber D, it is possible to establish in that chamber a temperature suitably elevated with respect to that in chamber B; and if necessary, further thermal sources (not shown) may be suitably arranged within this chamber and may be used e.g. when overheated steam is required to ll chamber D.

It is also possible to establish in chamber D predetermined pressure with respect to the outside because of the hydraulic closure formed by liquid sheet G.

After having proceeded along the horizontal portion 44 of the conveyor, the folds are carried onward by the ascending portion 45 of the upper reach of the conveyor 44 and are lifted up onto roller 48 which straightens the folds and conveys the slubbing in which the dye has been completely fixed to device F without subjecting the same to stretching.

While passing through device F, the slubbing is washed by waterfall G whereupon it passes between rollers 50 which pull it out of the steaming station.

Attention is drawn to the fact that the peripheral speed of outlet rollers 50 is equal to that of inlet rollers 10, whereas the speed of conveyor 44 is adjusted as desired through a speed control. Of course, this speed should be at most equal to the travel rate of the slubbing in chamber B; otherwise fold formation in duct 40 would be impeded.

Change of the speed of conveyor 44 permits varying the form of the folds of the slubbing in zone A2 and also varying the time during which each fold remains inside chamber D, and consequently the desired total duration of the fixing treatment.

In practice, the time during which the folded slubbing remains in chambers B and D together is varied from a minimum of 3 minutes to a maximum of 45 minutes.

In order to decrease the amount of humidity in chamber D, it is only necessary to lower the level of the liquid therein as determined by the upper end of overflow S6, through opening drain 87.

It is thus possible to secure in chamber D temperatures above 100 C., independent of the temperature prevailing in chamber B, because the outlet of duct 40 is practically closed by both folded slubbing coming out from said duct, and flap 43 striving to close the opening 42.

It is to be understood that the present invention is susceptible of several changes and modifications; for example, internally of chamber B may be disposed other heating sources to increase the action of the steam as let in through connector 38.

The sealing effect at slot 28 prior to the introduction of slubbing A into chamber B may be obtained through suitable sealing members consisting of, for example, rollers.

The apparatus according to the invention avoids the drawbacks of known apparatus. For instance, the excessive height required for Itube devices is avoided due to the fact that the curved duct 40 can be kept much shorter. On the other hand, it is surprising that complete fixation can be attained in chamber D in spite of the large empty space about the material being fixed, while the attainment of complete fixation is not surprising in the case of a column of material in a narrow .l -tube which is built up to a high level.

Another advantage offered by the apparatus according to the invention is the facility of providing a perfectly saturated steam-atmosphere in the large chamber D, since satisfactory fixing requires fully saturated steam which is particularly difficult to maintain with wool. Overheating can be avoided in the fixing chamber D for instance by blowing slightly overheated steam through the water sump in the bottom of that chamber. Superheating of the steam is also possible by the conventional Superheating means provided in the apparatus.

It could also not be foreseen that padded slubbing which had been laid in folds as is the case in the second zone A2 in the apparatus according to the invention, could be treated on the conveyor and drawn off without producing undulating color effects. Another advantage of the apparatus according to the invention resides in the fact that the width of the slubbing being treated can be much larger than is the case in the known J-tubes.

A further important advantage of the apparatus accordng to the invention lies in the avoidance of mechanical stresses on the slubbing being fixed during a stage in which it is particularly susceptible to such stresses. While, in the known I-tubes the folded material must travel with friction on the walls of the tube over a considerable length of the way, such travel with mechanical friction of the folded material is reduced to a fraction, due to the fact that the deflecting duct can be held much shorter, while during the entire treatment with steam in fixing zone A2, i.e. during the longer of the two fixing periods, the folded material is carried on the conveyor free from any friction or other mechanical stresses. This stress-free treatment helps to avoid undesirable felting of the folded slubbing and yields a finished material which is better spinnable than the material obtained by known stream-treatments.

The cleaning of the pre-fixing chamber and the deflecting duct in the appartus according to the invention is much easier than that of the J-tube.

EXAMPLE 1 Wool slubbing, standard color depth 1 25 parts of a red dyestuff of the formula:

25 parts of an orange chromium complex dyestufr` of the formula:

CHsSIOz @warp-CH.

n Ho /N 6.25 parts of blue dyestuif of the formula:

t te

CH3 NH-CO CHzCl are dissolved in 500 parts of hot water and 200 parts of a 5%-aqueous thickener consisting of etheried carob bean gum, and 40 parts of a mixed anionic/non-ionogenic dye assistant consisting of a mixture of 45% of sodium lauryl-diethylenoxy-sulfate, 45% of coconut oil fatty acid N,Nbisethanolamide and 10% of isopropanol, are added to the resulting solution, Thereto 100 parts of a 10% formic acid solution are then added and the whole is made up with water to 1000 parts. The temperature should be 40 C.

Wool slubbing is impregnated with the resulting 40 warm solution and sequenced out so as to leave 100% by weight of dye liquor on the slubbing, calculated on the weight of the latter. The slubbing is then treated in the horizontal steam apparatus according to the invention as shown in FIGURE 4, which comprises a 700 mm. high pre-fixing chamber, a curved duct section, the curvature of which describes an angle of about 60 against the vertically disposed central axis of the pre-fixing chamber, and a subsequently arranged second fixing chamber, which is provided with a conveyor belt, the part of the upper reach of which extends horizontally from the discharge opening of the curved duct section to the discharge means at the end wall of the second fixing chamber, is about 280 cm. long and the upwardly inclined end part of which upper reach is about 45 cm. long and rises at an angle of 34. The padded slubbing is introduced into the pre-fixing chamber at a speed of meters per minute without contacting any part of the pre-fixing chamber. The slubbing passes through this chamber under its own weight during 8 seconds without touching any part of the pre-fixing chamber and is subjected therein to saturated steam having a temperature of about 98-100 whereafter the pre-steamed slubbing is laid into folds in the curved duct section The folded material advances under its own weight towards the exit of the curved portion, the 60 curvature of said portion causing the horizontal folds to be gradually tipped into a near vertical position in which they remain on the upper reach conveyor belt, being transported through the second fixing chamber, for about 20 minutes; when passing upward on the inclined upper reach portion, they are tipped lightly backward upon the succeeding folds, whereby they are easily lifted off the conveyor belt by the discharging roll.

The second fixing chamber is also filled with saturated steam of about 98100 C. while the folded goods pass there through.

Thereafter, the thus treated slubbing is withdrawn from the second fixing chamber, washed with water in the back washing machine and air-dried.

The slubbing is now dyed a uniform, dark red color which shows no sandwich effect and is approximately of standard depth 1.

EXAMPLE 2 Nylon slubbing-light color Example l is repeated, using nylon 66 slubbing in lieu of wool slubbing, and

5 parts of the chromium dyestuff of the formula:

in lieu of the dyestuff used in Example 1. The slubbing passes at a speed of 7 meters per minute through the pre-fixing zone and remains for 10 minutes in the second fixing chamber. Steam conditions in both zones are the same asin Example 1. The color depth is somewhat higher than in the case of Example 1.

12 EXAMPLE 3 Wool slubbing-light color Example 1 is repeated but the dyestuff used therein is replaced by 5 parts of the dyestuff of the formula:

" SOzCH; COO CH3 G 1e@ @New COO CH4 SOZCHa The wool slubbing passes at a rate of 7 meters per minute through the pre-fixing zone and is steamed for 10 minutes in the second fixing chamber. A awless light grey dyeing is thus obtained.

`EXAMPLE 4 By repeating Example l, but using instead of the dye assistant used therein 50 parts of a mixture of 35 parts of sodium nonylphenol-diethyleneoxy-sulfate and 15 parts of coconut oil fatty acid N,Nbishydroxy ethyl-amide, practially the same product is obtained as that of Example l.

EXAMPLE 5 By repeating Example 1, but using instead of the dye assistant given therein an equal amount of sodium lauryl sulfonate there is obtained a level dyeing free from sandwich effect and of about 60% greater depth of shade than that of Example l.

EXAMPLE 6 20 parts of chromium dyestuf of the formula:

H HO

are dissolved in 400 parts of hot water. To the resulting solution are added 200 parts of aqueous 2% carob bean flour solution as thickener and 30 parts of the dye assistant used in Example l. To the whole are added 200 parts of a aqueous 10%-acetic acid and the resulting liquor is diluted to a volume of 1000 parts by the addition of water. The temperature of the liquor is raised to 45. Nylon 66 slubbing is impregnated with this solution and sequeezed out to retain a dye liquor absorption. Then the same steaming procedure as in Example 1 is followed. The material is washed in the backwashing machine in a known way, and then dried.

A very level, well fixed brilliant red dying is thus obtained.

EXAMPLE 7 By repeating Example 6, but using instead of the dye assistant given therein, an equal amount of 35 parts of sodium nonylphenol-diethyleneoxy-sulfate and 15 parts of coconut oil fatty acid N,Nbishydroxy ethyl-amide and instead of the acetic acid, 20 parts of ammonium sulfate, equally good red dyeings are obtained.

EXAMPLE 8 By repeating Example 6, but using instead of the 14 EXAMPLE 11 By repeating Example 10, but using in lieu of the dye assistant given therein an equal amount of the product obtained by condensing, at 150-200, coconut oil fatty acid dye assistant given therein `an equal amount of the prodand diethanol amine in a molar ratio of 1:2, there is obuct obtained by condensing, at 15G-200, coconut Oil tained an equally good blue dyeing on polyacrylonitrile fatty acid and diethanolamine in a molar ratio of 1:2, t0w

there are obtained similarly satisfactory level red dye- EXAMPLE 12 mgs' EXAMPLE 9 10 0.54 part of the dyestuif of the formula By repeating Example 6, but using instead of Nylon gi-CH3 66 slubbing, Nylon 66 tow, a level red dying is obtained /Cm 2,1013. on said tow. N\N/ N=NN\ EXAMPLE 10 15 (im ons( 3.5 parts of the. dyestuf of the formula a 0.88 part of the dyestuff of the formula s oHtO /mm i N=N 'N\ 7 C1 J1 \N/ oHsoHzoH s 3 parts of the dyestuf of the formula g3 S l I CHS CHS and 2.1 parts of the dyestuif of the formula N\N LN=N DN zno1s- /s CHF( Omo e CH3 30 C=NN=N ZnCla" and 27 parts of the dyestuff of the formula \N/ H3 rs oHxo- /CQH Hs N=N N ZnCls- \CHZCH2OH 35 are mixed to a paste with 60 parts of aqueous 80% acetlc If@ acid in the cold, and the paste is dissolved in 500 parts of CH; hot water. are mixed with 60 parts of aqueous ,80%'acetic acid in 200 Parts 0f a stock thlckener Conslstlng of aqueous 2% the cold to form a paste, which is dissolved in 500 parts carob bean ilour solutlon and 30 parts of the dye asslstant of hot water 40 used in Example 7 are added thereto.

200 parts of stock thickener consisting of aqueous 2% The v mole 1S 'brought uP to a Volume of 1000 p arts b y carob bean flour solution and 30 parts of the dye assistant me addltmn 0f Water and me temperatme Pf me liquor 1S usedin Example7are added raised to 45. Polyacrylonltrile slubblng 1s impregnated The whole is diluted to a volume of 1000 parts by the with this solution and squeezed out to retain a 180% dye addition of water. The temperature of the liquor is brought 45 llquol' absofpflolf and men ffeated 1n the Steam'tfeatmg to 45 Polyacrylonitrile tow is impregnated with this soluapparatus Wmch 1S descrmed m Example The travel mm tion and squeezed out to retain a dye liquor absorpof the Smbmng 1s 7 meters P er mmm? m me Pre'xmg tion The Polyacrylonitrile fibers used in this and subse zone and 1t1s treated for l5 minutes, slightly super'heated quent examples have a polymerization degree of about steam of a temperatm'e of 104106 bemg apphed m bom 35,000 and contain about 46 millimoles of SO3H and 50 Zones v 17 minimales of -CooH groups psrgloo g, of fibers. A Very Saflsfacfofy llght fa Shade 1S Obtamed- The acrylic material is moved at a.trave1 rate of 5 me- EXAMPLE 13 ters per minute through the pre-ixingcham-ber of the same apparatus as used in Example 1 and then steam treated for Similar .resuits .are Obtained Whe? repeatmg. Example 30 minutes in .the Second xing chamber, with Slightly 55 12, but using m heu of the dye assistant used 1n that exsuper-heated steam of a temperature of 104-106 being ampe Se same amount of the dye asslstant used m EX' used in both treatment chambers. amp e EXAMPLE 14 A tow dyed a very satisfactory navy blue shade is obtained. 2 parts of the dyestuff of the formula COOH COOH N t i t HZN- f soH 00H, on NH2 Coon Hogs? NH2 H 1103s sOsH E 15 16 2 parts of the dyestuff of the formula as that used in Example 14, and similar dyeings of navy Ho--N=NOH 0H Hooi) 1iI=N COOH:

SOgH are dissolved in 250 parts of hot water and mixed with blue shade and equally satisfactory properties are ob- 100 parts of an aqueous 2% carob bean our thickener tained as in that example. stock solution. To the resulting mixture, 5 parts of the dye 25 EXAMPLE 17 assistant used in Example 1 are added and the whole is brought up to a volume of 1000 parts by the addition of water. The temperature of the liquor is brought to 45.

Viscose slubbing is impregnated with this liquor, squeezed out to retain a 100% liquor absorption and then 30 Example 16 is repeated, but 5 parts of the dye assistant used in Example 7 are used in lieu of the dye assistant used in Example 1. Similar satisfactory results are obtained.

steamtreated in the apparatus which is described in Ex- EXAMPLE 18 ample 1. In this apparatus, the slubbing has a travel rate Example 14 is repeated, but in lieu of viscose slubof 6.5 meters per minute in the pre-fixing chamber and bing, viscose tow is dyed, with similar satisfactory reremains in the second xing chamber for 15 minutes, sults.

saturated steam of a temperature of 98-100 being 35 EXAMPLE 19 applied in both treatment chambers.

The slubbing is then treated in the back-washing machine at a speed which allows contact with a coppering bath to last for at least 15 seconds.

A very satisfactory level light tan shade is obtained. 40

Viscose tow is dyed by strictly following the procedure of Example 18 but using S parts of the dye assistant used in Example 7 in lieu of the dye assistant used in Example 1. Similar results as in Example 18 are obtained.

EXAMPLE 15 EXAMPLE 20 Viscose tow is dyed by strictly following the procedure Similar results are obtained by repeating Example 14, of Example 16, and goods of similar satisfactory navy but using, in lieu of the dye assistant used therein, 5 parts blue shade are obtained. of the dye assistant used in Example 7. 45 EXAMPLE 21 EXAMPLE 16 Viscose tow is dyed by strictly following the procedure Example 14 is repeated, but instead of the dyestuf of Example 17, and goods of similar satisfactory navy blend used therein, 20 parts of a dyestul of the formula blue shade are obtained.

OH OCE: OCHa 0H COOH COOH N02 NO3 and 10 parts of the dyestui of the formula COOH 2 are used and steam-treated, the goods passing at a rate I claim: of 4.5 meters per minute through the pre-fixing chamber 1. In a process for pad-dyeing slubbing or tow mateand being steamed for 30 minutes in the second fixing rials, which process comprises chamber; saturated steam of 98-100 is used in both (a) saturating a slubbing or tow material with at least chambers. In al1 other respects the procedure is the same 75 one bath of padding liquor,

17 (b) squeezing the material out to remove excess liquor therefrom, and (c) fixing the dye deposited on the fibers of said textile material by a treatment with steam,

the improvement consisting essentially f (i) subjecting the squeezed material during a downward movement thereof through a first zone in a loose state and free from any mechanical contact to a first thermal treatment with saturated steam, to prefix the treating bath components on the fibers of the material to such a degree that no substantial amounts of dye are left capable of migrating along the fibers of the impregnated material,

(ii) deiiecting the prefixed material gradually from its downward path to a substantially horizontal movement While causing the material simultaneously to form uniform folds, and

(iii) subjecting the prefixed and folded material during its subsequent horizontal movement through a second zone in which the folds are in substantially vertical position, to a second, separate thermal treatment with steam, while substantially blocking exchange of heating medium between the first and second zones of treatment.

2. The improvement as defined in claim 1, wherein the folds of said material are positioned in substantially vertical position at entering and during the major following part of their travel through said second zone.

3. The improvement as defined in claim 1 wherein the folds of said material are tipped backward under their 18 own weight during a minor, final part of their travel through said second zone.

4. The improvement as defined in claim 1, wherein the travel rate of the said textile material ranges from about 4 to 8 meters in said first zone and each fold of said material is present for from about 15 to 30 minutes in said second zone depending on the depth of shade desired thereon.

5. The improvement as defined in claim 1, wherein the textile material is polyamide fiber material, the heating medium in said first zone is saturated steam of from about 98 to 102 C. and the heating medium in said second zone is saturated to superheated steam having a temperature of about 100 to 103 C.

6. The improvement as defined in claim 1, wherein the textile material is acrylic fiber material and the heating medium in said first and second zones is superheated steam of temperature of about 102 to 107 C.

References Cited UNITED STATES PATENTS 2,395,305 2/ 1946 Vincent et al. 68-5 3,213,470 10/1965 Yasawa et al 8-152 DONALD LEVY, Primary Examiner U.S. Cl. X.R.

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