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Publication numberUS3692089 A
Publication typeGrant
Publication dateSep 19, 1972
Filing dateDec 3, 1970
Priority dateDec 3, 1970
Also published asCA949724A, CA949724A1
Publication numberUS 3692089 A, US 3692089A, US-A-3692089, US3692089 A, US3692089A
InventorsPrivott Wilbur Jr, Sargent Michael R
Original AssigneeMonsanto Co
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Process for controlling orifice size when extruding molten materials
US 3692089 A
The size of the orifice in a process for extruding low viscosity melts is controlled by maintaining at a predetermined level the partial pressure of a gas which enters into chemical reaction with the molten material contained within the crucible assembly, the materials comprising the crucible assembly, and the impurities contained in the melt.
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Description  (OCR text may contain errors)

United States Patent Privott, Jr. et a1.


, Micha Sar ent, a XLtN- Assignee: Monsanto Company, St, Louis, Mo.

Filed: Dec. 3, 1970 Appl. 190.; 94,720

US. Cl ..164/66, 164/82 Int. Cl. ..B22d 11/12, B22d 23/00 Field of Search ..164/66, 67, 82, 259;

1151 3,692,089 1451 Sept. 19, 1972 Primary Examiner-R. Spencer Annear Attorney--Vance A. Smith, Russell E. Weinkauf, John D. Upham and Neal E. Willis [57] ABSTRACT The size of the orifice in a process for extruding low viscosity melts is controlled by maintaining at a predetermined level the partial pressure of a gas which enters into chemical reaction with the molten material contained within the crucible assembly, the materials comprising the crucible assembly, and the impurities contained in the melt.

4 Claims, '4 Drawing Figures PROCESS FOR CONTROLLING ORIFICE SIZE WHEN EXTRUDING MOLTEN MATERIALS BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to a method of forming fibers directly from melts of low viscosity, and, more particularly, to a method of controlling orifice size when extruding molten materials of low viscosity through the orifice.

2. Discussion of the Prior Art The recent introduction of new techniques of forming fibers from melts of extremely low viscosity, i.e., less than about poises, has proven to be highly satisfactory and economically competitive to older processes such as, for example, wire drawing. One of the new techniques is described and claimed in detail in US. Pat. No. 3,216,076 issued on Nov. 9, 1965, to Alber et a]. Described therein is a method by which metals may be extruded as a free filamentary molten stream into a gaseous atmosphere and solidified into a fiber. To prevent surface tension from breaking the molten stream up into discrete spherical bodies, the gaseous atmosphere reacts with the stream to form an oxide film about the stream. The oxide film has sufficient strength to prevent surface tension-induced disruptions in the stream continuity prior to solidification of the stream into a fiber. This technique is called stabilizationd.

The Alber patent further states that certain metal oxide films are soluble in the molten metal stream and therefore are not suitable to prevent or retard stream disruptions due to surface tensions. The patentees teach the addition to the melt of a small quantity of a second metal having an oxide not soluble in the stream. Thus, for example, iron (or steel) has oxides which are soluble in the molten metal, but through the addition of a small quantity of aluminum, an insoluble aluminum oxide film may be formed about the stream to preclude continuity disruptions.

In the referenced application, it is taught that molten streams may also be stabilized by forming films other than oxides, such as, for example, nitride or carbon films. The method claimed therein has the additional advantage of not requiring the presence of a second metal in those instances wherein the predominant metal has a soluble oxide. The application further demonstrates that stabilization techniques are not limited to metals but may be used in forming fibers fromother low viscosity materials such as metalloids, metal oxides, and salts.

THE PROBLEM It has been observed that when certain molten materials, particularly the metals, are extruded through a small opening such as an orifice, precipitates often form in or near the orifice. This problem becomes highly significant when forming fibers in accordance with the stabilization techniques described above. The precipitate products in or near the orifice may cause undesirable lateral deviations of the molten stream after it has been extruded through the orifice and generally culminates in complete orifice plugging.

Chemical reactions occurring during the extrusion process are largely responsible for the partial or complete plugging of the orifice with the precipitate products. For example, in the extrusion of steel, the reaction is generally believed to be a refractory metaloxygen-refractory metal oxide reaction. Because it is necessary to use crucible assemblies comprised of materials which have both a high melting point and good thermal shock properties, certain refractory metal oxides such as alumina (A1 0 and beryllia (BeO) are often employed. Aluminum itself is often used in small quantities as a second metal to stabilize a molten stream of steel. Reactions occur between these materials, the oxygen, and the carbon in the molten steel. A gas such as carbon monoxide is released and begins to accumulate above the melt. Eventually, oxides such as chrysoberyi and alumina precipitate in or near the orifice causing the plugging problem. Chrysoberyl is beryllium aluminate,(BeO A1 0 and generally is found in a mixed system where both alumina and beryllia parts contact the melt.

It is therefore desirable to prevent or control changes in the orifice size due to the chemical reactions occur -ring between the melt, the impurities in the melt and the materials comprising the crucible assemblies.

SUMMARY OF THE PRESENT INVENTION Briefly, the present invention involves preventing undesirable changes in the size of an orificeor alternately controlling the size of the orifice while extruding a molten material contained in the crucible assembly through the orifice. In one aspect of the present invention, the partial pressure of a gas species which enters into the chemical reaction with the molten material contained within the crucible assembly, the materials comprising the crucible assembly, and the impurities contained in the melt is maintained at a predetermined level sufficient to thermodynamically equilibrate the chemical reaction. For example, in the extrusion of molten steel contained in an alumina crucible, with carbon monoxide being released above the melt, a flow of inert gas is used to remove the carbon monoxide as it is formed thereby thermodynamically equilibrating the chemical reaction.

Still another aspect of the present invention is the alteration of the size of the orifice during the extrusion process. Thus, by increasing or decreasing the partial pressure of the gaseous species to a selected predetermined level, orifice size may be increased or decreased as desired.

In describing the present invention, it is convenient to couch the description in terms of extruding molten steel. It will be apparent after a reading of the subject matter contained herein that the invention is adapted to the extrusion of other metals and other low viscosity materials in which a gaseous species enters into the reaction. Thus, the features believed to be characteristic of the present invention are set forth in the appended claims. The invention with further objects and advantages thereof may be best understood by reference to the following description taken in connection with the accompanying drawings in which:

FIG. 1 is a vertical cross-section of a typical spinning apparatus;

FIG. 2 is a graph depicting mass flow rate as a functionof extrusion time without an inert gas purge;

FIG. 3 is a graph depicting the mass flow rate as the purge flow rate is varied;

FIG. 4 is a graph of the mass flow rate as a function of time for a constant inert gas purge.

DESCRIPTION In the extrusion of molten steel, the process may be conducted either as batch or continuous extrusion. Batch extrusion is primarily the melting and extrusion of a single charge of steel as opposed to the continuous addition of charges in continuous extrusion. In batch extrusion, there is a general increase in the oxygen level as the process continues. There is also an increase in the amount of carbon monoxide in contact with and above the melt. It is believed that the following reactions take place in the melt:

MeO Me O -O C CO (2) where Me represents a metal such as aluminum, for example, and the underlined components represent components that are in solution. Combining Reactions (1) and (2),

MeO +C Me+C+O Me+CO 3 where MeO is the refractory oxide which under thermodynamically non-equilibrated conditions causing reaction (3) to proceed to the left may continually precipitate out of solution.

Because the orifice is open to a stabilizing chamber, thus usually cooler than the surrounding melt, precipitation when it occurs generally is in the vicinity of the orifice. At best, the presence of undesired precipitate particles in the orifice may affect the stream flow patterns which in turn affects stabilization, ultimately culminating in an inferior fiber. Generally, precipitate particles collect in the orifice until the orifice is filled or plugged, preventing stream flow.

We have found, however, that the orifice size may be kept essentially constant by thermodynamically equilibrating reaction (3). In other words, precipitation may be significantly reduced or eliminated. In general, the carbon and refractory metal concentrations in a single charge of molten steel are essentially constant. The melt temperature and carbon monoxide pressure level, however, are independent but interrelated variables. By controlling these two variables, reaction (3) may be kept thermodynamically equilibrated.

In accordance with one feature of the present invention, the gas species, for example, carbon monoxide, was removed by a flow of an inert gas, argon, for example, as it formed. By varying the rate of the carbon monoxide removal, the orifice size was altered as desired. That is, reaction (3) proceeds to the left when the carbon monoxide level is greater than the value at which reaction (3) is equilibrated. Under these conditions, the metal oxide precipitates in or near the orifice.

as to sweep away the gas formed due to the melt-crucible assembly reaction such as reaction (3). The rate of flow of the gas is controlled as desired to either maintain or alter orifice size. Other operations may use bubbling techniques to control orifice size. The term purging is therefore employed generically to define selective controlling of the gas species formed by the reaction to provide the proper partial pressure of the gas species. Thus, the term purging is unrestricted by the manner in which the gas species is removed.

EXAMPLE I A steel charge having about 1 percent aluminum was melted in a beryllia crucible assembly and held at a temperature of about l,650 C. The melt was then extruded through a 195 micron orifice at about 20 PSI into an oxide forming atmosphere such as, for example, air, carbon dioxide, or carbon monoxide. As Table 1 below illustrates the flow rate initially was about 63.4 gms/minute.

TABLE 1 Elapsed Time (min.) Flow Rate (gms/min.)

O 63.4 2.0 63.3 3.0 64.9 4.0 61.9 5.0 34.9 5.5 8.6 6.0 Flow stopped I The flow rate significantly decreased during the fourth minute and ceased at six minutes as demonstrated by the graph of FIG. 2. An examination of the precipitate which plugged the orifice determined that it was primarily composed of chrysoberyl.

EXAMPLE 2 A steel charge having about 1 percent aluminum was melted in a beryllia crucible assembly and held at a temperature of about 1,605 C. The melt was then ex truded through a micron orifice at an initial flow rate of about 23.0 gms/minute into an oxide forming atmosphere. Argon was used to purge the carbon monoxide which formed above the melt. Table 2 depicts the various elapsed time intervals, rate of argon purge, and mass flow rates of the molten steel. The graph of FIG. 3 illustrates the mass flow rate for the various elapsed time intervals.

Example 2 demonstrates that the flow rate of the mo]- ten material may be controlled by the rate of purge. As seen in FIG. 3, the flow decreased steadily for an argon purge of approximately 800 cc/min. This indicates that precipitation was occurring in the orifice. When the argon purge was increased to a value much greater then 800 cc/min., erosion of the orifice began to take place.

EXAMPLE 3 TABLE 3 Elapsed Time (min.) Flow Rate (gmslmin.)

21.50 streamed out From a reading of the description contained herein, it is clear that the present invention may be practiced with various molten materials being extruded through an orifice. Depending upon the result desired, the concentration of the gaseous species above the melt is maintained at a predetermined level resulting in close control of the orifice size. It will also be apparent that there are various ways in which the concentration of the gaseous species may be changed. it is to be understood that changes may be made in the particular features of the present invention which are within the full intended scope of the invention as defined in the following claims.

What we claim is:

1. In a process for extruding molten steel contained in a refractory metal oxide crucible assembly through an orifice wherein carbon monoxide enters into a chemical reaction occurring between the molten steel, the crucible assembly and impurities contained in the molten steel, the improvement which comprises maintaining the partial pressure of the carbon monoxide at a level which essentially thermodynamically equilibrates i l i'i i r r i ggvement of claim 1 wherein carbon monoxide is purged with an inert gas to maintain equilibrium.

3. The improvement of claim 1 wherein the refractory metal oxide is beryllia.

4. The improvement of claim 1 wherein the refractory metal oxide is alumina.

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US2907082 *Feb 6, 1956Oct 6, 1959Marvaland IncProduction of continuous filaments of high vapor pressure metals
US2976590 *Feb 2, 1959Mar 28, 1961Marvalaud IncMethod of producing continuous metallic filaments
US3216076 *Apr 30, 1962Nov 9, 1965Clevite CorpExtruding fibers having oxide skins
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3884289 *Aug 29, 1973May 20, 1975Monsanto CoInviscid spinning of silicon steel
US3946794 *Aug 29, 1973Mar 30, 1976Monsanto CompanyMethod for producing fine diameter wire from steel-titanium melts
US6585151May 23, 2000Jul 1, 2003The Regents Of The University Of MichiganMethod for producing microporous objects with fiber, wire or foil core and microporous cellular objects
US7626122Aug 27, 2007Dec 1, 2009David LevineLightweight composite electrical wire
US8697998Nov 30, 2009Apr 15, 2014David LevineLightweight composite electrical wire with bulkheads
US20080047736 *Aug 27, 2007Feb 28, 2008David LevineLightweight composite electrical wire
US20100071931 *Nov 30, 2009Mar 25, 2010David LevineLightweight composite electrical wire with bulkheads
U.S. Classification164/462
International ClassificationB22D11/00
Cooperative ClassificationB22D11/005
European ClassificationB22D11/00B