US2624189A

US2624189A - Apparatus for fluid treatment of filamentary materials

Info

Publication number: US2624189A
Application number: US2947A
Authority: US
Inventors: Pyam L Pendleton
Original assignee: HAMPTON MACHINE Co
Current assignee: HAMPTON MACHINE Co
Priority date: 1948-01-17
Filing date: 1948-01-17
Publication date: 1953-01-06
Anticipated expiration: 1970-01-06

Description

APPARATUS FOR FLUID TREATMENT OF FILAMENTARY MATERIALS Filed Jan. 17, 1948 Jan. 6, 1953 P. L. PENDLETON 2 SHEETSSHEET l Tilliili x E i INVENTOR.

Twm LPsupLsmu BY K ATTORNEY I Jan. 6, 1953 P. L. PENDLETON APPARATUS FOR FLUID TREATMENT OF FILAMENTARY MATERIALS Filed Jan. 17, 1948 2 SHEETS-SHEET 2 lNl/ENTOR TMM LTPENDLEroM ww y My ATTORNEV Patented Jan. 6, 1953 APPARATUS FOR FLUID TREATMENT OF FILAMENTARY MATERIALS Pyam L. Pendleton, Cranston,

Hampton Machine Company,

Rhode Island R. 1., assignor to a corporation of Application January 17, 1948, Serial No. 2,947

8 Claims.

This invention relates to the fluid treatment of filamentary materials.

More particularly, the invention concerns an apparatus for the treatment with active or inert fluids of one or more traveling strands or threads of textile fibers, or of an artificial filament, or bundle of artificial filaments, after formation by extrusion and coagulation.

In treating such materials, it is often desirable to apply the treating solution thereto under conditions of considerable pressure in order to achieve a more rapid, thorough and economical permeation thereof by the fluid or to induce a high and favorable circulation of the fluid in the vicinity of the material. For such purposes it has been heretofore proposed to provide within a sealed chamber a confined body of fluid, fluid pressure producing means and means for introducing and withdrawing the strand or filament from the fluid pressure zone without excessive fluid leakage. Such a structure must, of necessity, be adapted to withstand considerable pressures over a relatively large interior surface area of the chamber and be provided with complex sealing members to permit passage of the strand while preventing escape of fluid. p 7

It is an object of the present invention to provide an apparatus for fluid treatment of continuous strands of traveling filamentary materials whereby in an open bath or vat of treating fluid a zone of relativelyheavy fluid pressure may be created and a strand passed therethrough without the use of pressure retaining seals, covers or the like, the portion of the bath outside the pressure zone being under atmospheric pressure.

It is a further object of the invention to provide an apparatus for fluid impregnating or permeating of filamentary materials whereby a traveling continuous strand may be submerged in treating fluid open to atmospheric pressure, and while submerged, traverse a pressure zone in which the fluid pressure is usefully raised in the vicinity of the material to a degree over and above the static head with the rise in fluid pressure accompanied by a useful circulation of the fluid.

It is a further object of the invention to provide an apparatus of the type described containing a. semi-restricted submerged area in which the fluid pressure may be substantially raised by means of multiple fluid pressure jets discharging into the area in the. vicinity of the material under treatment and where by arranging the jets in opposed pairs the impact of the jets against the material will be balanced so that harmful'collision or frictional contact of the material against the boundary faces of the area will be avoided.

It is a further object of the invention to provide in an apparatus of the type described fluid pressure jets discharging into a channel with the interior faces of the channel acting to forcibly deflect and eject fluid from the channel after contact with the material.

It is a further object of the invention to provide in an apparatus of the type described a treating zone in which the application of fluid pressure to the material is of a rapidly pulsating nature, this being accomplished by causing the material to traverse a semi-restricted channel containing localized opposed pressure jets in alternate series with .localized channel sections from which the jets are forcibly deflected, the result being a pumping action in the close vicinity of the filament favorable to the cross sectional flow of the treating fluid.

Another object of the invention is to provide an apparatus for the high pressure fluid treatment of filamentary materials wherein the yarn or filament to be treated may be readily initially threadedthrough the apparatus, or re-threaded after breakage. With filaments of suflicient strength there would be no necessity of shutting down or reducing the fluid pressure during the re-threading operation. With very weak filaments simple valve control of the fluid would be the only accessory operation beyond the temporary shutting down of mechanisms arranged to traverse the material through the apparatus, which would be a requirement in all. cases.

It is also an object of the invention to provide a fluid treating apparatus having a fluid pressure zone created by opposing high velocity streams in which the passage of a strand therethrough may be assisted, retarded or neutrally affected by changing the angle of fluid impact or the fluid pressure or both to achieve a positive, negative or neutral tensile stress in the strand. It is to be understood that in the relief of tensile stress on the filament caused by passage through the apparatus which may be had by properly arranging the jet pressure and jet impact angle lies one of the principal features of the apparatus whereby yarn filaments may be fluid processed at extremely high speeds without being subject to damaging tensile stresses.-

It is a principal object of the invention to provide in a fluid treating apparatus of the type described means for permitting the apparatus to act as a storage device in which the angle of impact of fluid pressure jets in a pressure channel would be locally altered to accelerate the material under the treatment at the entrance end of the pressure channel and to decelerate or retard the flow of material at the exit end of the channel, the result being a compression or storage of the material in the channel while in process and a realization of the useful benefits of such storage as exemplified in the class of devices known as storage reels.

It is a general object of the invention to employ in a fluid processing apparatus a plurality of mutually opposed fluid streams to cause thefluid more rapidly and eifectively to permeate a continuous traveling strand of textile fibers or other filamentary material and to simultaneously control the movement of the strand through the apparatus, thereby providing in the combination a more convenient and practical means of fluid processing textile strands at high speeds and high fluid pressures than has been known heretofore.

A feature of the invention is the "creation within a trough or channel-like member by means of a plurality of opposed high velocity streams of fluid and without the necessity for pressure retaining seals or covers of a zone of relatively high fluid pressure through which the filamentary material may be passed, said troughlike member being open to atmospheric pressure permitting the high velocity streams to diffuse and 'well up therein after contact with the material and to drain therefrom by gravity, said streams being so directed that a resultant of pressure arising from collision and deflection serves to assist in the retention of the filamentary materials in said pressure zone.

Other objects and features will become readily apparent from the following detailed description taken in connection with the accompanying drawings in which there is illustrated a preferred embodiment of -the invention.

In the drawings:

Fig. 1 is a top plan view partly in section of the apparatus;

Fig. 2 is a vertical section viewon line 2-2 of Fig. 1;

Fig. 3 is a transverse section on line of Fig. 2;

Fig. lis a similar section on line 2-55 of Fig. '2;

Fig. 5 is a section in elevation showing in greater detail the bafiie structure at the ends of the apparatus with the removable baiiie plates in place;

Fig. 6 is a sectional view'on line of Fig. 5;

Fig. '7, is a fragmentary plan view of a modification of a portion of the apparatus shown in Fig. 1; and

Fig. 8 is a fragment'ary plan view showing an arrangement of jets to facilitate the use of the device as a storage apparatus.

The form of device illustrated in Figs. 1 to 6 comprises an open trough it; having fixed baflie plates 52 at either end and drains S4 at the bottom thereof. Jet carrying manifold-like members it and idare releasably aflixed by

bolts

28 and 22 respectively to the bottom interior of the trough it in parallel spaced relation. The member it is hollowed out to provide enlarged ducts 2 having a series of aligned outlet ports or jets directed inwardly into the longitudinal slot 28 between the members ES and I8. The member 53 is provided with similar ducts 3E} and similar ports 32, said ports, when members it and [8 are bolted in place, providing diametrically opposed jets adapted to emit high velocity streams of treating fluid which will converge at a plurality of points along the path of strand travel in slot 23. Member i8 is also provided with a longitudinal groove 28' of slight depth, mating with and forming a continuation of slot 28, for a purpose hereafter described.

In the bottom of the trough iii there are formed two longitudinal ducts or chambers 3e mating with the corresponding chambers 24 formed in members is. Corresponding chambers 36 are provided to supply fluid to ducts or chambers 36 in member I8.

Inlet pipes

38 and 40, connected to a source of liquid supply under pressure (not shown), in turn furnish treating fluid under any desired pressure to the

chambers

34 and 36, and through ducts 2d and 30 for emission in opposed streams from the

jets

26 and 32.

As shown in detail in Figs. 5 and 6, the ends of the trough It) are provided with a battle construction to permit entry and exit of the traveling strand 44 with a minimum of fluid loss. The end structure comprises a series of fixed parallel bafile plates l'2, spaced to interfit with removable bafile plates [3 carried in parallel spaced relationship by a supporting member [5. The plates l2 are provided with vertical slots48 and have substantially the configuration shown in Fig. 4. The removable plates l3 have substantially the configuration illustrated in Fig. 6 and are adapted to be inserted between the plates IE to provide a series of baflies having a plurality of openings 42 aligned with 'th'e bottom portion of the slot 28 so that the filament or yarn 44 may be passed in either direction directly through the trough Ill. Fluid passing with the strand 44 from the trough I!) through the restricted openings 42 will be wipedfrom thestrand by the bafile plates and drain by "gravity through auxiliary drains 46. In the treatment of some materials it may be preferable to adjust the relation'ship of the

plates

12 and 13 in such a manner that the openings 42 form a sinuous path or labyrinth through which the strand must pass whereby the volume of fluid carried through the bafiies by the traveling strand may be substantially reduced. 7

It should be pointed out in this connection that other types of sealing closures may be subs'tituted for the specific bafile system herein described for use at the ends of the trough l0, and the filament or strand may be introduced or withdrawn from the trough in in any suitable manner. For example, I may avoid theuse of any strand passage openings below the liquid level in the trough by passing the strand downwardly into the trough and under submerged rollers, pulleys or rods and withdrawing it in a similar fashion so that leakage is effectually eliminated. Such an arrangement, however, lacks the e'ase'of threading of the embodiment illustrated in the drawings.

It is a particular advantage of my invention that the treating fluid need not be confined under high pressure in a treating chamber but may be allowed to well up freely in the slot 28 and in the open trough ll) so as to drain by gravity through the drains l4 and 46 which are of sufficient cross-sectional area to accommodate any desired volume of fluid emitted by the jets. Thus, at the ends of the trough near the baiiles, the fluid is no longer under high pressure and consequently the amount of leakage will be greatly reduced. 7

I In this manner I'have "provided an apparatus in which a strand may be treated with relahigh pressure.

tively heavy fluid pressure. of say 100 lbspperv square inch, but which possesses none of the ordinary drawbacks incident to the use of such Thus heavy pressure resisting construction, complex closures to permit the introduction and withdrawal of yarn and yet prevent leakage, difliculty of access to for the purpose of cleaning and threading, etc., are all eliminated by my novel apparatus and method.

In the operation of the according to the invention, I may supply treating fluid, of whatever type maybe desirable for the particular impregnating or washing treatment involved, through the

inlet pipes

38 and 40. Before introducing the fluid, member 15 is lifted out together with the removable bafile plates I3 affixed thereto, leaving a series of aligned openings constituting a narrow longitudinal slot extending the entire length of the trough. A strand or filament 44 may then be threaded from above through the slot 28 into groove 28 and the plates [3 replaced. The yarn will continue to enter and leave the apparatus through the openings 42 while treating fluid, welling up in the trough, is drained through the outlets l4 and 4E. The accumulated discharge from the jets will cause a rise of fluid in the trough ID to some point below its upper edge. There the accumulated static head, as related to the depth of the fluid in the trough l and the cross-sectional area of the drains l4, will cause the fluid to flow out the drains as rapidly as it enters through the

jets

26 and 32 and thereby maintain a liquid level sufficient to submerge the members i6 and [8 but not to overflow the edges of the trough l0.

Groove 28' is of sufficient depth so that the center of strand 44 is located below the center of the opposed fluid streams from the jets, although preferably not deep enough to remove the strand below a position of direct exposure to the streams. In this manner, the resultant downward pressure on the strand of the meeting, balanced, mutually deflecting streams, is greater than the upward pressure thereon, and lifting ofthe strand in or out of the slot 28 bythe upward force and flow of the fluid is prevented.

the filament 44 be passed through the apparatus of Figs. 1 to 6 from left to right in Fig. 1, the impacts of the liquid streams ejected through the jets 2B and 32 at an acute angle to thepath of travel serve to propel the filament through the apparatus. If the filament is'passed in the reverse direction, the streams through the jets .are at an obtuse angle to the path of travel of the filament, so that the filament is retarded by the impacts of the high pressure streams of fluid. Drafting rollers or other suitable means may be provided at the outlet end of the trough to tension the filament against the retarding effect of rearwardly directed jets, such tension being desirable for certain operations such as washing of causticized yarn in a mercerizing process. In all cases the accelerating or decelerating effect of the streams may be altered by regulating the fluid pressure.

If desired, the manifold members is and 18 may be made easily removable by the use of readily

accessible bolts

20, 22. Interchangeable manifold members may be provided to replace the members It and i8, such additional manifolds having ports directed at any desired angle. For example, as shown in Fig. 7, a neutral drafting effect may be obtained by arranging the ports fluid treating device the interior- 26" and 32 to direct streams of fluidat right angles to the path of travel of the yarn.

The slots 48 in plates 12 are made very narrow for the treatment of strands or filaments of small diameter. For example with yarns having a diameter of not more than .01", the slots should be no more than .015" wide. The slot 28 between the manifold members is preferably also of similarly narrow width, only slightly in excess of the diameter of the filament or filaments being treated, although the slot should be of substantial depth.

Since there is no problem of retaining the fluid at high pressure the trough I0 may preferably remain open at the top throughout its length to facilitate cleaning and threading the strand, although a cover is optional. The fluid discharged willbe effectively retained without. the usev of elaborate sealing closures and need not be shut 01f or reduced in pressure for re-threading in case of breakage of the strand unless the strand is of an extremely delicate nature. By arranging the

ports

26 and 32 to discharge opposing streams and by narrowly confining the strand in the channel 28 so as to travel along a path defined by the points of impact of the streams, a balanced pressure condition is attained which reduces contact of .the strand with the edges of the slot and protects the strand from disruptionby the high velocity streams or by frictional engagement with the walls of the slot.

Where a series of manifold-members is used as in multiple process operations, the jets may number atotal of several hundred. In such an apparatus, if the ports are set at 90 to thepath of travel of the strand, the total fluid friction on the strand may attain undesirable proportions. In these cases the jet angle can be modified forwardly to offset the effect of friction so that no effort is required to draw the strand through high pressure zones between the manifold members It and [8 whose combined length might total, for example, as much as or 40 feet. Thus the strand may be processed under high fluid pressure while the longitudinal stress within the strand is kept substantially at zero.

Where it is desired time during which the yarn remains under fluid treatment or in other words to cause the apparatus to function as a storage device, the port impactangles may be varied in a single system asat. 49, '50 and 5| in Fig. 8 where the yarn is accelerated by ports 29 upon entrance from a free running supply at a rate greater than the acceleration produced by ports 5! which have a greater angle of incidence. The result is a tendency of the yarn to accumulatein the pressure zone which may be slightly enlarged as at 52 and in which the ports would supply no'acceleration but would be arranged to retain the yarn in the pressure zone in this section.

A moving strand passing through the trough encountering successive streams discharged at high pressure, will also pass through small areas of lower pressure between the streams, resulting in a favorable pulsating pressure condition conducive to effective permeation or washing. When the traveling strand passes through the zones near the drains M the fluid pressure will become very light, and when it enters the baffle system fluid will drain therefrom by gravity.

In my apparatus the strand is subjected simultaneously to a substantial static pressure of the body of treating liquid in the trough and a high kinetic pressure of the fluid streams projected to increase the length of I 7 against the yarn. These combined pressures; together with the pulsating action of the kinetic pressure, produce a marked improvement over prior apparatus and methods in the efficiency of the action of treating fluids on filaments, strands, threads and yarns.

I have illustrated the invention as applied to the treatment of a single strand in a single passage between the manifolds but it will be understood that strands may be passed in multiple between a single pair of manifolds, or a single strand may be reversed on itself and passed back and forth between a single pair of manifolds. In either case, the number of lengths of strand passed between the manifolds at one time is preferably low in order that the width of the treating slot between the manifolds may be kept small.

Itwill therefore be seen that I have provided a new and improved apparatus for applying a treating fluid to filamentary materials under high pressure for the more convenient and effective permeation or impregnation thereof. In the foregoing description and the accompanying drawings I have disclosed a preferred embodiment of the invention, but it is to be understood that modifications and changes may be made therein by persons skilled in the art within the spirit and scope of my invention as defined in the appended claims.

I claim:

1. Apparatus for the high pressure liquid treatment of a traveling strand of filamentary material without harmfully disrupting the same, which comprises: a trough adapted to contain a bath of treating liquid at substantially atmospheric pressure, a manifold mounted within said trough, conduits for supplying treating liquid under high pressure to said manifold, said manifold having a pair of substantially vertical closely spaced opposing walls extending longitudinally within said trough and said trough having an upwardly facing surface beneath and intersecting said walls and defining therewith a narrow longitudinally extending channel, said manifold having a series of submerged ports arranged in line in each wall for admitting treating liquid to said channel, the ports of one of said series facing corresponding ports of the other series so that the resulting pairs of opposed jets will mutually impinge upon and counteract each other, said ports likewise being close to said upwardly facing surface where= by the portion of said channel substantially be tween said surface and the region defined by the points of mutual impact of said opposing jets and bounded by the intermediate portions of said walls will constitute a narrow longitudinal treating zone of high liquid pressure through which said strand may travel in the direction of its length.

2. Apparatus according to claim 1 in which at least some of said pairs of opposing jets are directed at right angles to the path of strand travel.

3. Apparatus according to claim 1 in which at least some of said pairs of opposing jets are directed at an obtuse angle to the path of strand travel.

4. Apparatus according to claim 1 in which at least some of said pairs of opposing jets are angled in the direction of strand travel for impelling said strand forwardly through said treat-- ing zone.

5. Apparatus according to claim 1 in which at least some of said pairs of opposing jets are angled ina direction opposite to that of strand travel whereby the forward movement of said strand of treating liquid 8 will be retarded by the impacts of said jets, and in which said apparatus includes a device for drawing said strand through said treating zone against the resistance of said jets.

6. Ap aratus according to claim 1 in which the ends of said trough comprise a series of spaced parallel slotted interfitting bafiie members, the slots thereof being of different shapes but portions of the same being aligned with each other to provide a leak resistant opening at each end of said trough permitting the introduction and withdrawal theretlirough of the traveling strand, the edges of at least the slots at the outlet end of Said trougn being arranged successively to contact said strand on different sides thereof and to wipe surplus liquid therefrom after it leaves said treating zone.

7. Apparatus for the high pressure liquid treatment of a traveling strand of filamentary material without harmfully disrupting the same, which comprises: a trough adapted to contain a bath of treating liquid at substantially atmospheric pressure, a pair of manifolds mounted within said trough, conduits for supplying treating liquid under high pressure to said manifolds, said manifolds being elongated and substantially parallel to each other and having opposed vertical closely spaced walls defining, with the bottom of said trough, a narrow longitudinally extending channel, said manifolds providing two opposed series of submerged ports in said walls for the admission of treating liquid to said channel, each of said seriesbeing arranged in line in its corresponding wall and the ports of one series facing corresponding ports of the other series sothat the resulting opposed pairs of jets will mutually impinge upon and counteract each other, said ports likewise being close to the bottom of said trough whereby the portion of said channel between said bottom and the points of mutual impact of said opposing jets and bounded by the intermediate portions of said walls will constitute a narrow longitudinal treating zone of high liquid pressure through which said strand may travel in the direction of its length.

8. Apparatus for the high pressure liquid treatment of a travelingstrand of filamentary mate rial without harmfully disrupting the same, which comprises: a trough adapted to contain a bath at substantially atmospheric pressure, a pair of manifolds mounted within said trough, conduits for supplying treating liquid under high pressure to said manifolds, said manifolds being elongatcd and substantially parallel to each other and having opposed vertical closely spaced walls, said trough having an upwardly facing surface beneath and intersecting said walls and defining therewith a narrow longitudinally extending channel, each of said manifolds pro-- viding an aligned series of submerged ports in its corresponding wall for the admission of treat ing liquid to said channel, the ports of one series facing corresponding ports of the other series so that the resulting opposed pairs of jets will ..mutually impinge upon and counteract each other, said ports likewise being close to thebottom of said channel whereby the portion of said channel between said bottom and the points of mutual impact of said opposing jets and bounded by the intermediate portions of said walls will constitute a narrow longitudinal treating zone of high liquid pressure through which said strand may travel in the direction of its length, the ends of said trough being spaced from the ends of said manifolds and comprising a series of spaced parallel slotted interfitting baffle members, the slots thereof being of different shapes but portions of the same being aligned with each other to provide a leak resistant opening at each end of said trough permitting the introduction and withdrawal therefrom of traveling strand, the edges of at least the slots at the outlet end of said trough being arranged to contact said strand on different sides thereof and to wipe surplus liquid therefrom after it leaves said treating zone, said trough being further provided with drains between the ends of said manifolds and said baffles.

PYAM L. PENDLETON.

REFERENCES CITED The following references are of record in the file of this patent:

Number 15 Number 10 UNITED STATES PATENTS Name I Date Meikle Mar. 16, 1886 'Lyth Jan. 10, 1922 De Jahn et a1 Apr. 22, 1930 Nieman Dec. 31, 1935 Schlumpf June 27, 1939 Ferm Mar. 5, 1940 Gonser et a1 Dec. 3, 1940 Hill et al Oct. 20, 1942 Ufnowski Mar. 2, 1943 Bond May 11, 1948 FOREIGN PATENTS Country Date Great Britain 1884