US3856074A - Method of centrifugal production of continuous metal filaments - Google Patents

Method of centrifugal production of continuous metal filaments Download PDF

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US3856074A
US3856074A US00348814A US34881473A US3856074A US 3856074 A US3856074 A US 3856074A US 00348814 A US00348814 A US 00348814A US 34881473 A US34881473 A US 34881473A US 3856074 A US3856074 A US 3856074A
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filament
wheel
quenching
nipping
tension
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S Kavesh
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Allied Corp
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D11/00Continuous casting of metals, i.e. casting in indefinite lengths
    • B22D11/06Continuous casting of metals, i.e. casting in indefinite lengths into moulds with travelling walls, e.g. with rolls, plates, belts, caterpillars
    • B22D11/0637Accessories therefor
    • B22D11/0694Accessories therefor for peeling-off or removing the cast product

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  • the present invention relates to an improvement in the production of continuous metal filaments of indefinite length which are normally wound on spools. More specifically, for the purposes of the invention, filament is herein used to represent a slender body whose trans-.
  • the filaments may be ribbons, sheets, wires or irregular cross-sections.
  • Melt extraction connotes a process wherein a cold quenching wheel rotates at high velocity in kissing, i.e., skimming, contact with a liquid metal surface.
  • the molten metal wetting the wheel is'carried up out of the molten bath, where it solidifies and thereby shrinks away from the wheel and is flung off by centrifugal action.
  • the melt extraction techniques discussed herein are to be distinguished from other extraction methods such as those described in U.S. Pat. No. 1,025,848 to Wagner and U.S. Pat. No. 2,074,8l2 to Sendzimer, which primarily employ a casting technique in which the cold wheel is substantially immersed in the liquid metal and in which the rotational velocity of the wheel is appreciably lower than in the melt extraction.
  • Chill block spinning is exemplified by U.S. Pat. No. 905,758 to Strange and Pirn, U.S. Pat. No. 2,825,108 to Pond, U.S. Pat. No. 2,886,866 to Wade,and U.S. Pat. No. 2,899,728 to Gibbons.
  • a free jet of molten material is impinged upon a moving chilled quenching surface, preferably a rotating wheel.
  • the molten jet is solidified in the form of a ribbon or sheet and is flung away from the rotating chill surface by centrifugal action.
  • melt extraction and chill block spinning processes as presently employed is that they produce long, but not genuinely continuous filaments.
  • the flinging action which removes the filament from the wheel induces an oscillating or whipping motion in the filament which inevitably causes breakage.
  • filaments are produced with a maximum length of only about 300 meters.
  • Continuous metal filaments in the range of" 1,000 to greater than 30,000 meters in length are required for such applications as strapping, springs, filament-wound vessels, aerospace skins and the like.
  • this invention is directed to an improvement in the production of metal filaments, ribbons or sheets.
  • the improvement comprises establishing a tension-free zone by positioning a pressure exerting means in nipping contact with the quenching source beyond the point of solidification; ideally, just at the point where shrinkage of the filament causes detachment from the quenching source.
  • the filament can then be directed from the nipping means and wound on a tension controlled winder or other collecting means such as a spinning bucket.
  • the nipping action isolates the fragile filament or sheet in the solidification zone from the tension exerted by the winder.
  • the continuoustension exerted by the winder and/or tension regulating mechanism used in conjunction with the winder prevents whipping, thereby avoiding filament breakage and enabling production of a truly continuous filament.
  • the nipping means employed may be any device having freedom of movement and capable of exerting sufficient pressure on the solidifying filament to counteract the stress transmitted by the winder and also by inherent centrifugal and gravitational forces thereby preventing breakage.
  • the device may be in the form of a bar, a blunt blade or preferably, a cold wheel freely rotating or driven at the same surface velocity as the quench wheel.
  • the role of the nipping device is not merely that of a guide. It is intrinsic to this invention that pressure be exerted by the device onto the solidifying filament and not merely that the filament be guided around the device.
  • the mere positioning of a guide wheel at the point of solidification does not prevent breakage of the filament since it does not counteract the centrifugal or gravitational forces or the tensional stress transmitted by the winder.
  • the arrangement of the invention requires, as an essential facet, freedom of movement so that the nipping device can readily adapt to use in forming filaments of various thickness and does not ficients of friction between the filament and the quench roller and the filament and the nip roller respectively.
  • This novel method for producing continuous wound filaments could be easily adapted to any process for preparing filaments in which the quenching step is carried out on a chill wheel, drum, etc. and the filament is separated after solidification by centrifugal force.
  • This method is particularlyuseful in very high speed forming operations where formation and subsequent winding occurs very rapidly and a great amount of stress is transmitted to the solidifying filament.
  • FIG. 1 illustrates diagrammatically an apparatus which uses a wheel melt extraction in conjunction with DESCRIPTION OF THE PREFERRED EMBODIMENTS
  • FIGS. 1 and 2' are representative of the novel aspects of the present invention.
  • a cold wheel rotates in kissing contact as shown at 12 with surface -17 of a liquid metal 18 confined in a suitable reservoir 11.
  • the molten metal solidifies on the surface 19 of the wheel 10 and is carried up out of the reservoir 11, and at a point 13 at which it begins to shrink away from the wheel 10 it comes into contact with a second cold wheel 14 which exerts a nipping pressure (between wheels 10 and 14) on the filament 15.
  • the filament 15 is then continuously drawn by a conventional tension control device 16 and wound onto' a roller 17.
  • the position of the nipping roller 14 and the pressure which it exerts on the filament 15 are controlled by means of a pressure exerting mechanism such as an air cylinder operating-through a conventional connecting link betweenthe roller 14 and the cylinder (not shown).
  • the nipping roller 14, as shown in FIG. 1a is swivelled to a remote position.
  • Rotation of the quenching wheel 10 is initiated and the level of liquid metal 18 in the reservoir 11 is raised by opening a valve from a supplemental reservoir (not shown).
  • a valve from a supplemental reservoir (not shown).
  • formation of the metal filament commences.
  • the filament is flung away by centrifugal action at the point 13 and the nipping roller 14 is then converged toward quenching wheel 10 so that the filament 15 is held between these rotating elements and the filament is conveyed via a tension control regulator 16 to a winder.
  • the pressure exerted by the nipping roller 14 on the filament 15 isolates the fragile solidification zone 12 to 13 from the tension of the winding arrangement and prevents filament breakage from this source and/or from whipping of the filament as it is drawn by the winder.
  • the metal filament 15 is then continuously wound up in packages whose lengths are determined only by the capacity of the winder. Molten metal is admitted to the reservoir '11 to maintain the continuous filament forming process.
  • Moderate changes in the rotational speed of the quench roller 10 or changes in the thickness of the filament do not substantially affect the winding process or continuity of the filament.
  • an air cylinder or other suitable positioning and/or pressure applying device may be used to. hold the nip roller against the quench roller thereby permitting the filament thickness to vary without reduction of nipping pressure.
  • FIG. 2 an alternate apparatus is employed to provide a similar result.
  • the melt 28 is contained in an insulated container 29 provided with heating element 31.
  • the nipping roller 24 is swiveled to a remote position in a manner as described in connection with FIG. la.
  • Rotation of the quenching wheel 21 is initiated and inert gas 34v is admitted to the melting container or vessel 29.
  • a molten jet 32 is extruded from a suitable opening 33 in the bottom of the container 29 and impinges upon the rotating quench wheel 21 to form a filament 30.
  • the filament has a tendency to be flung away by centrifugal action at that point 23.
  • the nipping roller 24 is converged on wheel 21 and the solidified filament 25 is conveyed to a tension controlled windbar 26 to a storage roller 27 as previously described in connection with FIG. 1.
  • the nipping rollers 14 and 24 are preferably freely rotating, lightweight devices supported byroller bearings. They may comprise a solid cylinder, a hollow cylinder, or a composite cylinder.
  • a desirable configuration has been foundto be a composite hollow cylinder having an outer shell consisting of a material of a high coefficient of friction bonded to an inner annular tube the present invention are any materials which are wear resistant under the temperatures of use.
  • Illustrative examples include organic impregnated woven asbestosbrass wire compositions manufactured by Raybestos- Manhattan Corporation and designated as U898 and US2010.
  • the inner core may be steel or similar high strength material.
  • the wind-up mechanism may be used alone or in conjunction with a separate tension regulating device as 16 and 26. If the wind-up mechanism is used alone, it should contain a means of regulating tension as for example by means of a slip clutch on the winding drum. Alternatively, separate tension regulating devices may be employed; illustrative devices could be counterbalanced, spring-loaded or balanced by means of an air cylinder.
  • EXAMPLE 1 A grey iron alloy containing 3.4 weight percent carbon, 2.2 weight percent silicon, 0.6 weight percent manganese, 0.2 weight 'percentphosphorus and 0.01 percent sulfur was melted at l,200 C.- in a conventional apparatus for melt extraction similar to that depict'ed schematically in FIG. 1. However, a nip roller similar to roller 14 was not utilized.
  • the quenching wheel was constructed of oxygen free high conductivity copper of 8 inch outside diameter and provided with internal channels for thecirculation of cooling water. Cooling water was admitted through a rotary union on one. side of the hollow quenching wheel shaft and was withdrawn through a rotary union on the opposite side. The face width of the quenching wheel was one inch.
  • Rotation of the quenching wheel was commenced at 1,800 revolutions per minute.
  • the level of the grey iron melt in the crucible was raised by opening a valve to the connecting reservoir.
  • the liquid metal surface was brought into kissing contact with the rotating quench wheel.
  • a solidified filament of .1 inch width and 0.000l-0.008 inch thickness was formed on the face of the quench wheel and was flung away by centrifugal action.
  • the arcuate. path of the solidified filament commenced at a tangent to the surface of the quenching roll, traveled upward at an angle of 30 60 to the horizontal, reached a point of maximum elevation and finally turned downward and fell into a catch basin on the floor.
  • the path of the filament was severely affected by whipping oscillations induced by random changes in the point and angle of departure of the filament from the quench roll.
  • the filament remained continuous for periods of several seconds until at irregular intervals the oscillations caused the filament to break off near the quench roll.
  • the filament was seized near the point of departure from the quench roll and guided to engage the winder. At filament tensions of ll grams filament oscilla- 6 ribbon 1 inchwide by 0.008 inch thickness were produced for eight hours without experiencing a break.
  • Example 2 The apparatus of Example 1 was modified by utilizing a nipping roller 14 as depicted in FIG. 1.
  • the nipping roller was of 4 inch overall diameter and consisted of a 4 inch diameter hollow steel cylinder of one-quarter inch wall thickness.
  • the nip roller was of 2 inch face width and was supported by a one-half inch steel shaft mounted on roller bearings. It was freely rotatable.
  • EXAMPLE 3 An alloy formulated to be amorphous upon quenching was charged in an apparatus for chill block spinning similar to that depicted schematically in FIG. 2. However, no nip roller was provided. The quenching wheel iron, 39- atomic percent nickel, l4 atomic percent phosphorus, 6 atomic percent boron and 3 atomic percent aluminum. It was melted in an argon atmosphere at l,000 C. The quench wheel was set into motion at 1,800 rpm and the molten alloy extruded through an orifice of 0.010 inch diameter at 300 cm/sec'. The molten jet traversed a 1 inch air gap and impinged upon the surface of the rotating quench wheel.
  • a solidified filament 0.025 inch wide by 0.002 inch thick was formed and was flung away by centrifugal action.
  • the path of the solidified filament commenced at a tangent to the surface of the quench wheel, traveled downward at an angle of 3060 to the horizontal and terminated on the laboratory floor.
  • the filament was seized near the point of departure from the quench roll and guided to engage the winder. Attempts were made without substantial success to wind the filament continuously under controlled tension. At filament tensions of l-l 0 grams filament oscillations persisted causing eventual breakage. During the periods between breaks, only an unsatisfactorily loose filament winding was produced. With higher winding tensions the filament was torn apart in the solidification zone immediately as it was connected to the winder.
  • Example 4 The apparatus of Example 3 was modified by provision of a nipping roller depicted as 24 in FIG. 2.
  • the nipping roller 24 was of 4 inch overall diameter and consisted of a 4 inch diameter hollow steel cylinder of -24.
  • the nip roller was then actuated to the closed or converged position as shown in FIG. 2. by means of an air cylinder (not shown) which pressed the filament against the quenching wheel with a force of pounds. This pressure was chosen by reference to equation (1) as explained below.
  • the filament was seized as it passed through the nip zone and guided to engage the winder. The filament was then continuously wound without interruption at l-pound tension. Tight uniform packages of metal ribbon 0.025 inch wide by 0.002 inch thickness were produced for 8 hours without experiencing a break.
  • T 1.0 lbs/in.
  • the nip roll pressure was set at 5 pounds.
  • the improvement which comprises exerting sufficient nipping pressure on, the formed filament at a point on-the quenching wheel beyond the point of solificiation of the filament and prior to the point said filament is separated from the quenching wheel by centrifugal action to retain the filament against the quenching wheel and subsequently collecting the filament.
  • T is the winding tension in lbs/inch of filament width and ,u and m are coefficients of friction between the filament and quenching wheel and the filament and nip roller respectively.

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  • Mechanical Engineering (AREA)
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Abstract

A method for producing and concomitantly winding continuous metal filament in which a quenching wheel is used as a quenching element and in which sufficient pressure is exerted on the filament just beyond the point of solidification to counteract the tensional stress exhibited by the winder on the filament.

Description

United States Patent Kavesh Dec. 24, 1974 [5 METHOD OF CENTRIFUGAL PRODUCTION 989,075 4/1911 Staples 164/276 01: CONTINUOUS METAL FILAMENTS 2,172,018 9/1939 Spencer 164/87 D UX 3,677,481 7/1972 Haley et al 164/82 X Inventor: Sheldon Kai/98h, PP y 3,812,901 5/1974 Stewart et al 164/87 [73] Assignee: Allied Chemical Corporation, New FOREIGN PATENTS OR APPLICATIONS York 1,040,766 9/1966 Great Britain .1 [64/82 [22] Filed: Apr. 6, 1973 Primary Examiner-R. Spencer Annear [21] PP 348,814 Attorney, Agent, or FirmArthur J. Plantamura 52 us. 01 164/87, 164/276, 264/164 1 1 ABSTRACT [51] Int. Cl B22d 11/06 A method for producing and concomitantly winding [58] Field of Search 164/87, 276, 278; 264/ 164, continuous metal filament in which a quenching wheel 264/165 is used as a quenching element and in which sufficient pressure is exerted on the filament just beyond the [56] References Cited point of solidification to counteract the tensional UNITED STATES PATENTS stress exhibited by the winder on the filament. 745,786 12/1903 Cole 164/276 4 Claims, 3 Drawing Figures K; '4 NIPP1NG PRESSURE 10 o PATENTED 1153241974 3, 856.074 sum 1 i 2 PRESSURE NIPPING METHOD OF CENTRIFUGAL PRODUCTION OF CONTINUOUS METAL BACKGROUND OF THE INVENTION The present invention relates to an improvement in the production of continuous metal filaments of indefinite length which are normally wound on spools. More specifically, for the purposes of the invention, filament is herein used to represent a slender body whose trans-.
verse dimensions are much less than its length. In the present context, the filaments may be ribbons, sheets, wires or irregular cross-sections.
During recent years, researchers developed various methods'directed to the formation of metal filaments which avoid the inherent difficulties' of previous casting and rolling techniques. These methods include, for example, melt extraction and chill block spinning.
Melt extraction connotes a process wherein a cold quenching wheel rotates at high velocity in kissing, i.e., skimming, contact with a liquid metal surface. The molten metal wetting the wheel is'carried up out of the molten bath, where it solidifies and thereby shrinks away from the wheel and is flung off by centrifugal action. The melt extraction techniques discussed herein are to be distinguished from other extraction methods such as those described in U.S. Pat. No. 1,025,848 to Wagner and U.S. Pat. No. 2,074,8l2 to Sendzimer, which primarily employ a casting technique in which the cold wheel is substantially immersed in the liquid metal and in which the rotational velocity of the wheel is appreciably lower than in the melt extraction.
Chill block spinning is exemplified by U.S. Pat. No. 905,758 to Strange and Pirn, U.S. Pat. No. 2,825,108 to Pond, U.S. Pat. No. 2,886,866 to Wade,and U.S. Pat. No. 2,899,728 to Gibbons. In this process, a free jet of molten material is impinged upon a moving chilled quenching surface, preferably a rotating wheel. The molten jet is solidified in the form of a ribbon or sheet and is flung away from the rotating chill surface by centrifugal action.
one important disadvantage in the melt extraction and chill block spinning processes as presently employed is that they produce long, but not genuinely continuous filaments. The flinging action which removes the filament from the wheel induces an oscillating or whipping motion in the filament which inevitably causes breakage. Presently filaments are produced with a maximum length of only about 300 meters. Continuous metal filaments in the range of" 1,000 to greater than 30,000 meters in length are required for such applications as strapping, springs, filament-wound vessels, aerospace skins and the like. n
An additional problem encountered. in the melt extraction and chill block spinning processes is that of winding the lengths of filament formed. The incorporation of a tension regulated winder or similar collecting device intothe system results in, a great amount of stress being transmitted back to the solidification zone, a factor which, contributes to the breakage of the filaments. Since the down time caused by rethreading the filaments onto the winder after breakage is considerable, the metal filaments must be wound in a separate operation. There is obviously a need for a method to produce continuous lengths of metal filaments which can be wound concomitantly with production.
SUMMARY OF THE INVENTION It is therefore an object of this invention to produce continuous metal filament, or ribbon or sheet.
It is another object to produce a continuous filament or sheet which can be automatically collected in a neat coiled package concomitantly with its production.
These and other objects and advantages will become apparent from the description and examples provided herein.
Accordingly, this invention is directed to an improvement in the production of metal filaments, ribbons or sheets. In the production of these materials using a rotating wheel as the quenching source, the improvement comprises establishing a tension-free zone by positioning a pressure exerting means in nipping contact with the quenching source beyond the point of solidification; ideally, just at the point where shrinkage of the filament causes detachment from the quenching source. In an additional aspect of the invention, the filament can then be directed from the nipping means and wound on a tension controlled winder or other collecting means such as a spinning bucket. Thus, the nipping action isolates the fragile filament or sheet in the solidification zone from the tension exerted by the winder. The continuoustension exerted by the winder and/or tension regulating mechanism used in conjunction with the winder prevents whipping, thereby avoiding filament breakage and enabling production of a truly continuous filament.
The nipping means employed may be any device having freedom of movement and capable of exerting sufficient pressure on the solidifying filament to counteract the stress transmitted by the winder and also by inherent centrifugal and gravitational forces thereby preventing breakage. The device may be in the form of a bar, a blunt blade or preferably, a cold wheel freely rotating or driven at the same surface velocity as the quench wheel. In this regard, it is to be noted that the role of the nipping device is not merely that of a guide. It is intrinsic to this invention that pressure be exerted by the device onto the solidifying filament and not merely that the filament be guided around the device. The mere positioning of a guide wheel at the point of solidification does not prevent breakage of the filament since it does not counteract the centrifugal or gravitational forces or the tensional stress transmitted by the winder. The arrangement of the invention requires, as an essential facet, freedom of movement so that the nipping device can readily adapt to use in forming filaments of various thickness and does not ficients of friction between the filament and the quench roller and the filament and the nip roller respectively.
This novel method for producing continuous wound filaments could be easily adapted to any process for preparing filaments in which the quenching step is carried out on a chill wheel, drum, etc. and the filament is separated after solidification by centrifugal force.
This method is particularlyuseful in very high speed forming operations where formation and subsequent winding occurs very rapidly and a great amount of stress is transmitted to the solidifying filament.
While this application is directed to the use of the nipping pressure means in conjunction with the use of a tension regulating winder, itis obvious that the invention also includesthe production of long or continuous filaments which are not wound concomitantly with their production but are collected in another manner.
BRIEF DESCRIPTION OF THE DRAWING FIG. 1 illustrates diagrammatically an apparatus which uses a wheel melt extraction in conjunction with DESCRIPTION OF THE PREFERRED EMBODIMENTS FIGS. 1 and 2'are representative of the novel aspects of the present invention. In FIG. 1, a cold wheel rotates in kissing contact as shown at 12 with surface -17 of a liquid metal 18 confined in a suitable reservoir 11. The molten metal solidifies on the surface 19 of the wheel 10 and is carried up out of the reservoir 11, and at a point 13 at which it begins to shrink away from the wheel 10 it comes into contact with a second cold wheel 14 which exerts a nipping pressure (between wheels 10 and 14) on the filament 15. The filament 15 is then continuously drawn by a conventional tension control device 16 and wound onto' a roller 17. The position of the nipping roller 14 and the pressure which it exerts on the filament 15 are controlled by means of a pressure exerting mechanism such as an air cylinder operating-through a conventional connecting link betweenthe roller 14 and the cylinder (not shown).
During start-up of the process, the nipping roller 14, as shown in FIG. 1a is swivelled to a remote position. Rotation of the quenching wheel 10 is initiated and the level of liquid metal 18 in the reservoir 11 is raised by opening a valve from a supplemental reservoir (not shown). When the liquid metal 18 contacts the quench wheel 10, at the contact point 12, formation of the metal filament commences. The filament is flung away by centrifugal action at the point 13 and the nipping roller 14 is then converged toward quenching wheel 10 so that the filament 15 is held between these rotating elements and the filament is conveyed via a tension control regulator 16 to a winder.
The pressure exerted by the nipping roller 14 on the filament 15 isolates the fragile solidification zone 12 to 13 from the tension of the winding arrangement and prevents filament breakage from this source and/or from whipping of the filament as it is drawn by the winder. The metal filament 15 is then continuously wound up in packages whose lengths are determined only by the capacity of the winder. Molten metal is admitted to the reservoir '11 to maintain the continuous filament forming process.
Moderate changes in the rotational speed of the quench roller 10 or changes in the thickness of the filament do not substantially affect the winding process or continuity of the filament. As noted hereinabove, an air cylinder or other suitable positioning and/or pressure applying device may be used to. hold the nip roller against the quench roller thereby permitting the filament thickness to vary without reduction of nipping pressure. I
In FIG. 2, an alternate apparatus is employed to provide a similar result. In FIG. 2, the melt 28 is contained in an insulated container 29 provided with heating element 31. During start-up of the process, the nipping roller 24 is swiveled to a remote position in a manner as described in connection with FIG. la. Rotation of the quenching wheel 21 is initiated and inert gas 34v is admitted to the melting container or vessel 29. A molten jet 32 is extruded from a suitable opening 33 in the bottom of the container 29 and impinges upon the rotating quench wheel 21 to form a filament 30. The filament has a tendency to be flung away by centrifugal action at that point 23. The nipping roller 24 is converged on wheel 21 and the solidified filament 25 is conveyed to a tension controlled windbar 26 to a storage roller 27 as previously described in connection with FIG. 1.
The nipping rollers 14 and 24 are preferably freely rotating, lightweight devices supported byroller bearings. They may comprise a solid cylinder, a hollow cylinder, or a composite cylinder. A desirable configuration has been foundto be a composite hollow cylinder having an outer shell consisting of a material of a high coefficient of friction bonded to an inner annular tube the present invention are any materials which are wear resistant under the temperatures of use. Illustrative examples include organic impregnated woven asbestosbrass wire compositions manufactured by Raybestos- Manhattan Corporation and designated as U898 and US2010. The inner core may be steel or similar high strength material.
The wind-up mechanism may be used alone or in conjunction with a separate tension regulating device as 16 and 26. If the wind-up mechanism is used alone, it should contain a means of regulating tension as for example by means of a slip clutch on the winding drum. Alternatively, separate tension regulating devices may be employed; illustrative devices could be counterbalanced, spring-loaded or balanced by means of an air cylinder.
The invention will be further described in the following illustrative examples:
EXAMPLE 1 A grey iron alloy containing 3.4 weight percent carbon, 2.2 weight percent silicon, 0.6 weight percent manganese, 0.2 weight 'percentphosphorus and 0.01 percent sulfur was melted at l,200 C.- in a conventional apparatus for melt extraction similar to that depict'ed schematically in FIG. 1. However, a nip roller similar to roller 14 was not utilized.
The quenching wheel was constructed of oxygen free high conductivity copper of 8 inch outside diameter and provided with internal channels for thecirculation of cooling water. Cooling water was admitted through a rotary union on one. side of the hollow quenching wheel shaft and was withdrawn through a rotary union on the opposite side. The face width of the quenching wheel was one inch.
Rotation of the quenching wheel was commenced at 1,800 revolutions per minute. The level of the grey iron melt in the crucible was raised by opening a valve to the connecting reservoir. The liquid metal surface was brought into kissing contact with the rotating quench wheel. A solidified filament of .1 inch width and 0.000l-0.008 inch thickness was formed on the face of the quench wheel and was flung away by centrifugal action. The arcuate. path of the solidified filament commenced at a tangent to the surface of the quenching roll, traveled upward at an angle of 30 60 to the horizontal, reached a point of maximum elevation and finally turned downward and fell into a catch basin on the floor. The path of the filament was severely affected by whipping oscillations induced by random changes in the point and angle of departure of the filament from the quench roll. The filament remained continuous for periods of several seconds until at irregular intervals the oscillations caused the filament to break off near the quench roll.
The filament was seized near the point of departure from the quench roll and guided to engage the winder. At filament tensions of ll grams filament oscilla- 6 ribbon 1 inchwide by 0.008 inch thickness were produced for eight hours without experiencing a break.
The coefficients of dynamic friction for several metal systems are given by The Handbook of Chemistry and Physics, 51st Edition, pp. Fl5-F 17. The coefficient of friction between grey iron and steel is 0.4. The coefficient of friction between steel and a copper film (8 kg. load) is given as 0.2. Taking the latter to be the same as the friction coefficient between grey iron and copper, the necessary minimum nip roll pressure was obtained from equation (1) by making the following substitutions.
tions persisted causing eventual breakage. During the periods between breaks, only a relatively unsatisfactorily loosely wound filament was produced. With higher winding tensions the filament ruptured in the solidification zone immediately as it was connected to the winder.
EXAMPLE 2 The apparatus of Example 1 was modified by utilizing a nipping roller 14 as depicted in FIG. 1. The nipping roller was of 4 inch overall diameter and consisted of a 4 inch diameter hollow steel cylinder of one-quarter inch wall thickness. In addition, the nip roller was of 2 inch face width and was supported by a one-half inch steel shaft mounted on roller bearings. It was freely rotatable.
7 The melt'extraction process wasstarted with grey iron alloy as describedin Example 1. The nip roller 14 was swiveled to the remote position depicted in FIG. la, the path of the centrifugally flung filament passed above and between the quench roll and the nip roll. The nip roller was then actuated to the closed or converged position by means of an air cylinder which pressed the filament against the quenching wheel with a force of 30 pounds. This pressure was chosen by reference to equation (1) as will be explained below. The filament was seized as it passed through the nip zone and guided to engage the winder. The filament was then continuously wound without interruption at 10 pounds tension. Tight, uniform packages of grey iron T= l0 lbs/in Mun from equation (I) P a 16.67 lbs/in To provide a margin of safety, the nip roll pressure was set at 30 pounds.
EXAMPLE 3 An alloy formulated to be amorphous upon quenching was charged in an apparatus for chill block spinning similar to that depicted schematically in FIG. 2. However, no nip roller was provided. The quenching wheel iron, 39- atomic percent nickel, l4 atomic percent phosphorus, 6 atomic percent boron and 3 atomic percent aluminum. It was melted in an argon atmosphere at l,000 C. The quench wheel was set into motion at 1,800 rpm and the molten alloy extruded through an orifice of 0.010 inch diameter at 300 cm/sec'. The molten jet traversed a 1 inch air gap and impinged upon the surface of the rotating quench wheel. A solidified filament 0.025 inch wide by 0.002 inch thick was formed and was flung away by centrifugal action. The path of the solidified filament commenced at a tangent to the surface of the quench wheel, traveled downward at an angle of 3060 to the horizontal and terminated on the laboratory floor.
The filament was seized near the point of departure from the quench roll and guided to engage the winder. Attempts were made without substantial success to wind the filament continuously under controlled tension. At filament tensions of l-l 0 grams filament oscillations persisted causing eventual breakage. During the periods between breaks, only an unsatisfactorily loose filament winding was produced. With higher winding tensions the filament was torn apart in the solidification zone immediately as it was connected to the winder.
EXAMPLE 4 The apparatus of Example 3 was modified by provision of a nipping roller depicted as 24 in FIG. 2. The nipping roller 24 was of 4 inch overall diameter and consisted of a 4 inch diameter hollow steel cylinder of -24. The nip roller was then actuated to the closed or converged position as shown in FIG. 2. by means of an air cylinder (not shown) which pressed the filament against the quenching wheel with a force of pounds. This pressure was chosen by reference to equation (1) as explained below. The filament was seized as it passed through the nip zone and guided to engage the winder. The filament was then continuously wound without interruption at l-pound tension. Tight uniform packages of metal ribbon 0.025 inch wide by 0.002 inch thickness were produced for 8 hours without experiencing a break.
The coefficients of dynamic friction for several metal systems are given by The Handbook of Chemistry and Physics, 51st Edition, pp Fl5-Fl7. The coefficient of friction between cast iron and steel is 0.4. The coefficient of friction between steel and a copper film (8 kg load) is given as 0.2. Taking these to be the same as the friction coefficient between the alloy spun here and the necessary steel and copper, minimum nip roll pressure was obtained from equation (1) by making the following substitutions.
T= 1.0 lbs/in. F'QR MIR 04 from equation P z 1.0/0.2 +0.4 P 2 1.67 lbs/in.
To provide a. margin of safety, the nip roll pressure was set at 5 pounds. I
I claim:
1. In a method for the production of metal filaments from a molten source using a rotating quenching wheel as a quenching element, the improvement which comprises exerting sufficient nipping pressure on, the formed filament at a point on-the quenching wheel beyond the point of solificiation of the filament and prior to the point said filament is separated from the quenching wheel by centrifugal action to retain the filament against the quenching wheel and subsequently collecting the filament.
2. The method of claim 1 wherein the formed filament is directed onto a tension regulated winding device and the nipping pressure exerted is sufficient to counteract the tensional stress exhibited on the filament by the winder and to create a tension free zone in which continuous lengths of filament can be produced and concomitantly wound.
3. The method of claim 2 wherein the nipping pressure in lbs/inch exerted is at least as great as that derived from the equation:
where T is the winding tension in lbs/inch of filament width and ,u and m are coefficients of friction between the filament and quenching wheel and the filament and nip roller respectively.
4. The method of claim I- wherein the nipping pressure is exerted by a cold nipping wheel.
' g y UNITED STATES PATENT OFFICE 5 9 CERTIFICATE OF CORRECTION patent 3,856,074 Dated December 24. 1974 Inventor) Sheldon Kavesh It is certified that error appears in the above-identified patent and that said Letters Patent are hereby corrected as shown below:
Column 4, line 41, "or" should be of Column 2, line 60, the equation should read:
P T/(UQR UNR) Column 6, line 17, the equation should read:
- P i l0/(0.2 O. 4)
. Column 8, line 1, the equation should read:
Claim 3, column 8, line 26, the equation should read:
En'gncd and Scaled this seventeenth Day Of February 1976 [SEAL] Attest:
RUTH C. MASON C. MARSHALL DANN Arresting Officer Commissioner oflarems and Trademarks

Claims (4)

1. In a method for the production of metal filaments from a molten source using a rotating quenching wheel as a quenching element, the improvement which comprises exerting sufficient nipping pressure on the formed filament at a point on the quenching wheel beyond the point of solificiation of the filament and prior to the point said filament is separated from the quenching wheel by centrifugal action to retain the filament against the quenching wheel and subsequently collecting the filament.
2. The method of claim 1 wherein the formed filament is directed onto a tension regulated winding device and the nipping pressure exerted is sufficient to counteract the tensional stress exhibited on the filament by the winder and to create a tension free zone in which continuous lengths of filament can be produced and concomitantly wound.
3. The method of claim 2 wherein the nipping pressure in lbs/inch exerted is at Least as great as that derived from the equation: T/ Mu QR + Mu NR where T is the winding tension in lbs/inch of filament width and Mu QR and Mu NR are coefficients of friction between the filament and quenching wheel and the filament and nip roller respectively.
4. The method of claim 1 wherein the nipping pressure is exerted by a cold nipping wheel.
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FR2409312A1 (en) * 1977-09-12 1979-06-15 Sony Corp METHOD AND APPARATUS FOR THE MANUFACTURING OF AN AMORPHIC ALLOY BY ROLLING
DE2906814A1 (en) * 1978-03-03 1979-09-06 Nat Standard Co METHOD AND DEVICE FOR MANUFACTURING SOLID FILAMENT-LIKE OBJECTS
US4186245A (en) * 1978-09-28 1980-01-29 Allied Chemical Corporation Energy storage flywheel
US4202404A (en) * 1979-01-02 1980-05-13 Allied Chemical Corporation Chill roll casting of amorphous metal strip
US4256039A (en) * 1979-01-02 1981-03-17 Allied Chemical Corporation Armor-piercing projectile
US4326579A (en) * 1980-01-23 1982-04-27 National-Standard Company Method of forming a filament through melt extraction
US4331739A (en) * 1978-10-10 1982-05-25 Allied Corporation Amorphous metallic strips
US4380262A (en) * 1980-10-27 1983-04-19 Gte Laboratories Incorporated Apparatus for double roller chill casting of continuous metal foil
US4449568A (en) * 1980-02-28 1984-05-22 Allied Corporation Continuous casting controller
JPS6046846A (en) * 1976-10-22 1985-03-13 アライド―シグナル・インコーポレーテッド Manufacture of continuous strip of crystalline metal
GB2158746A (en) * 1984-05-14 1985-11-20 Olin Corp Apparatus and process for rolling spin cast strip
US4614220A (en) * 1984-11-16 1986-09-30 The United States Of America As Represented By The Secretary Of The Air Force Method for continuously casting thin sheet
US4649983A (en) * 1983-10-26 1987-03-17 Allied Corporation Chill roll casting of metal strip
US4916109A (en) * 1987-07-14 1990-04-10 Lonza Ltd. Catalyst for the oxidation of carbon compounds
US5550102A (en) * 1987-04-02 1996-08-27 Sumitomo Electric Industries, Ltd. Superconductor and method of manufacturing the same
US5647921A (en) * 1993-08-23 1997-07-15 Mitsui Petrochemical Industries, Ltd. Process for producing and amorphous alloy resin

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US989075A (en) * 1909-04-28 1911-04-11 Willard Griffin Staples Metal-strand machine.
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US745786A (en) * 1902-08-18 1903-12-01 Albert L Cole Machine for fibering metals.
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GB1040766A (en) * 1962-10-26 1966-09-01 Louyot Comptoir Lyon Alemand Improvements in methods of extrusion and wiredrawing of metallic products and devices for the practical application of said improved methods
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Cited By (19)

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Publication number Priority date Publication date Assignee Title
JPS615821B2 (en) * 1976-10-22 1986-02-21 Allied Corp
JPS6046846A (en) * 1976-10-22 1985-03-13 アライド―シグナル・インコーポレーテッド Manufacture of continuous strip of crystalline metal
FR2409312A1 (en) * 1977-09-12 1979-06-15 Sony Corp METHOD AND APPARATUS FOR THE MANUFACTURING OF AN AMORPHIC ALLOY BY ROLLING
DE2906814A1 (en) * 1978-03-03 1979-09-06 Nat Standard Co METHOD AND DEVICE FOR MANUFACTURING SOLID FILAMENT-LIKE OBJECTS
DE2906814C2 (en) * 1978-03-03 1988-09-29 Marvalaud, Inc., Westminster, Md., Us
US4186245A (en) * 1978-09-28 1980-01-29 Allied Chemical Corporation Energy storage flywheel
US4331739A (en) * 1978-10-10 1982-05-25 Allied Corporation Amorphous metallic strips
US4202404A (en) * 1979-01-02 1980-05-13 Allied Chemical Corporation Chill roll casting of amorphous metal strip
US4256039A (en) * 1979-01-02 1981-03-17 Allied Chemical Corporation Armor-piercing projectile
US4326579A (en) * 1980-01-23 1982-04-27 National-Standard Company Method of forming a filament through melt extraction
US4449568A (en) * 1980-02-28 1984-05-22 Allied Corporation Continuous casting controller
US4380262A (en) * 1980-10-27 1983-04-19 Gte Laboratories Incorporated Apparatus for double roller chill casting of continuous metal foil
US4649983A (en) * 1983-10-26 1987-03-17 Allied Corporation Chill roll casting of metal strip
GB2158746A (en) * 1984-05-14 1985-11-20 Olin Corp Apparatus and process for rolling spin cast strip
US4614220A (en) * 1984-11-16 1986-09-30 The United States Of America As Represented By The Secretary Of The Air Force Method for continuously casting thin sheet
US5550102A (en) * 1987-04-02 1996-08-27 Sumitomo Electric Industries, Ltd. Superconductor and method of manufacturing the same
US4916109A (en) * 1987-07-14 1990-04-10 Lonza Ltd. Catalyst for the oxidation of carbon compounds
US4978513A (en) * 1987-07-14 1990-12-18 Lonza Ltd. Catalyst for the oxidation of carbon compounds
US5647921A (en) * 1993-08-23 1997-07-15 Mitsui Petrochemical Industries, Ltd. Process for producing and amorphous alloy resin

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