Field of the Invention
[0001] The present invention relates to dust free, dry wire drawing compounds, and processes
for their manufacture, particularly to dry wire drawing compound lubricants characterized
as dry, free-flowing, non-powdery, non-dusty, compositions and constructions having
at least one reproducibly controlled dimension which form viscous lubricating films
directly or after reduction in size.
Background of the Invention
[0002] Wire drawing is a process employed to produce wire from rod by pulling the rod and
wire through one or more dies in order to reduce the cross-sectional area until a
final product of the desired cross-section is achieved.
[0003] "Rod" is a term used to denote hot-rolled, undrawn stock used in the wire drawing
process. "Wire" is the term used to denote the product of drawing, i.e., rod which
has been reduced in cross-sectional area.
[0004] Dies used in the wire drawing process must be of sufficient hardness to withstand
the pressure, heat, and abrasiveness developed by the wire passing through the die.
Most wire drawing dies are constructed of special alloys such as tungsten-carbide
or similar hard materials or alternatively, the die surfaces, which may contact the
moving wire, are coated with thermally stable, abrasion resistant coatings. Direct
contact between the die surface and the moving wire surface must be kept to a minimum,
or preferably prevented entirely, in order to maintain the desired surface characteristics
of the wire and prevent excessive die wear and damage.
[0005] Typical dies designed for wire drawing operations consist of four zones which may
be described as follows: Zone 1, or the approach zone, consists of a circumferential
angular opening encircling the moving wire which allows the wire drawing lubricant
to enter the die. The angle of the approach zone's interior surface, relative to the
moving rod or wire surface, is typically 6 degrees to 25 degrees. The selection of
approach zone angle depends on the size and composition of the wire to be drawn, draw
speed, number of reductions required, and lubricant formulation and physical form.
The lubricant must be in a form which allows it to enter the approach zone along with
the wire. Zone 2, or reduction zone, is the location within the die in which plastic
deformation of the rod or wire occurs. It is in Zone 2 that reduction of cross-sectional
area is achieved during drawing. Zone 2 is a continuous extension of Zone 1, encircling
the moving wire. The angle of the interior surface of Zone 2 relative to the moving
wire determines both the degree of cross-sectional reduction and is a major factor
in controlling the thickness of the wire drawing lubricant film which remains on the
wire surface as it exits the die. This residual lubricant is essential when a number
of dies are used in a series to effect multi-step cross-sectional reductions. Zone
3 is referred to as the bearing zone. It serves principally to assure final shaping
of the wire. Zone 4 is the pressure relief zone. Pressure developed between the wire
and die surfaces can reach many thousands of pounds per square inch during the drawing
operation. It is necessary that this pressure be released at the die exit in a manner
which avoids damage to the die. Without a pressure relief zone, cracking of the die
can occur.
[0006] Dies may be used in combination with a single die stand. These are referred to as
pressure dies and are designed to increase the pressure on the wire drawing lubricant
in order to force additional lubricant onto the surface of the wire and thus increase
the residual lubricant film thickness.
[0007] As noted above, it is essential that the rod or wire be prevented from coming in
contact with the die surface during wire drawing. This is accomplished by maintaining
a continuous film of lubricant between the die surface and the surface of the moving
wire. When dry wire drawing lubricants are used, the rod or wire is pulled continuously
through a bed of dry wire drawing lubricant contained in a "soap box" or "die box."
The soap box has an entry port and an exit port through which the wire passes. The
exit port of the soap box is comprised of a first die located such that the die is
below the surface level of the wire drawing compound contained in the soap box. Periodic
additions of wire drawing compound are made to the soap box to assure that its first
die is always submerged in wire drawing compound.
[0008] When a series of dies are employed for multi-step reductions, there may be additional
soap boxes associated with specific dies. The purpose of these additional boxes is
to supply additional surface lubricant coating to the wire if needed.
[0009] The wire being pulled through the die system travels at speeds of a few feet per
minute, up to thousands of feet per minute, depending on the die system, wire composition,
cross-sectional area reduction required, cooling capacity, and lubrication available.
At these high speeds it is necessary that the undrawn rod surface be roughened so
that lubricant in sufficient quantity will adhere to the surface and be carried into
the die. Roughening of the rod may be accomplished by applying chemical coatings to
the rod prior to its introduction into the wire drawing system. The most common coating
compositions are based on lime, borax, or phosphates. The resultant rough coating
is commonly referred to as a "lubricant carrier" coating.
[0010] Mechanically descaled rod may be sufficiently rough without further coating or, if
necessary, may be roughened with additional mechanical treatment.
Lubricant applicators can be used to force lubricant onto the rod surface by pressure.
[0011] The dry wire drawing compound lubricants must flow freely in the soap box in order
that fresh lubricant be exposed to the moving wire. If the wire drawing compound fails
to move freely by gravitational force or mechanical agitation in the soap box, it
will compact into a dense mass through which the moving wire will form a channel.
This is a condition known as "tunneling." Once tunneling occurs, there is a loss of
contact between the wire and the dry lubricant and, as a result, the die system is
starved for lubricant and damage to the wire and die surface will occur.
[0012] As the dry wire drawing compound lubricant enters the die at the approach zone, it
is converted by heat and/or pressure into a film of plastic-like consistency. If converted
to a liquid, it would offer little, if any, protection against the wire moving laterally
through it and contacting the die surface. Further, the majority of a liquid lubricant
applied to the wire in this type of drawing system would be lost immediately upon
exiting the die and would not be available as residual lubricant for protection of
other dies in a multi-die system.
[0013] The composition of the dry wire drawing compound lubricants has been discussed widely
in the patent and technical literature, some examples of which are set forth hereinafter
in the detailed description. In a broad sense, dry wire drawing compounds are typically
based on a combination of fatty acid soaps, excess base or free fatty acid, and, as
required for specific applications, various thickeners, pressure additives, pigments,
fillers, and thermal stabilizers. The most commonly used dry wire drawing compound
lubricants are based on calcium soaps or sodium soaps. A manufacturer of dry wire
drawing compound lubricants typically offers several hundred different formulations,
each designed to satisfy the technical requirements of specific wire drawing applications.
[0014] Historically, dry wire drawing compound lubricants have been produced as fine powders
in order to meet the stringent requirements of the wire drawing process. However,
these powdered materials are very dusty, lending to worker irritation and unclean
work areas.
[0015] Various approaches have been tried to alleviate the dust problems associated with
dry wire drawing compound lubricants. These include tableting, extruding, flaking,
beading, and wetting. None, however, have been totally successful.
[0016] Wetting of the compound with a liquid to suppress dustiness introduces a non-active
diluent which frequently has a deleterious effect on one or more essential properties
of the lubricant, such as lowering of the melt point or reduction in free flowability.
[0017] "Beading" is a process of manufacturing dry wire drawing compound lubricants disclosed
in Canadian patent 1,006,497. Although this patent discloses a composition which is
"essentially dust-free," it states that "the presence of fines in minor amounts ...
can be tolerated without loss of operating efficiency." In practice, these beaded
compositions are less than completely dust free as would be expected from the presence
of fine particles. Removal of the fines by screening or washing would add costly manufacturing
steps. Further, the beads formed by rolling are not uniform in dimension in any direction,
resulting in separation during shipment and use.
[0018] Flaking of dry wire drawing compound lubricants by casting a molten mass of the lubricant
onto a chill roll is essentially ineffective. The resultant flakes are too large,
typically one-half inch in diameter (12 mm), to perform effectively in wire drawing
systems. Grinding of the flakes to produce smaller particle size invariably leads
to production of a fine powder fraction and dust.
[0019] Tableting is an expensive process and, again, the particle size, typically one-quarter
inch in diameter (6 mm) or greater, is unsatisfactory.
[0020] Extruding of dry wire drawing compounds on conventional screw extruders, operated
in a conventional manner, such as are used in making pelletized plastics or plastic
additives has been tried in the dry wire compound lubricant industry without success.
While the pellets produced were dust free, the work energy required to form them hardened
the pellets so that they would not melt or reduce to useful size in the wire drawing
process.
[0021] It is completely surprising that the process of the instant invention solves all
of the problems of previous attempts at making effective, dust free, dry wire drawing
compound lubricants, especially since no permanent additional additives such as water-soluble
binders which could interfere with or change the lubrication properties of the dry
wire drawing compound lubricants are required.
Summary of the Invention
[0022] This invention pertains to a method for the manufacture of dust-free, dry wire drawing
compound lubricants and metal soap compositions having at least one reproducibly controlled
dimension which possess all of the beneficial properties of powdered lubricants and
none of the undesirable properties of powders, such as dust generation. The process
comprises the steps of conglutinating and shaping the dry wire drawing compound composition
under controlled pressure. The conglutinating and shaping steps may be performed sequentially
or simultaneously.
[0023] Materials used as raw materials in the process are dry wire drawing compounds, usually
in powder form, comprising metal soaps, unreacted basic compounds, free fatty acids,
and, as required for specific applications, minor amounts of various adjuvants such
as fillers, pigments, dyes, extreme pressure additives, stabilizers, thickeners, waxes
and polymers, esters, ethoxylates and metal wetting agents.
[0024] A wide range of temperature can be employed in the pressure forming step, with the
restriction that it is below the melt point of the metal soap component of the dry
wire drawing composition. At least one dimension of the shaped article formed by the
pressure forming step is reproducibly uniform.
[0025] A wide range of forming pressure energy may be employed with the proviso that it
be no greater than the energy later required to reduce the product of the process
to smaller particles during use by pulverizing, softening, or melting.
[0026] The most preferred application for the novel products of the invention is in wire
drawing through stationary or roller dies. As used herein terms such as "dust free"
or "non dusting" refer to the shaped wire drawing compound constructions which are
essentially free of dustable particulates as formed. Minor amounts of dustable particulates
may be generated during cutting operations to form the construction to the desired
length(s), but these may be readily removed, typically by exposing the construction
to a vacuum during the cutting operation.
Detailed Description of the Invention
[0027] A method has now been discovered for the production of conglutinated and shaped dust-free
dry wire drawing lubricant compounds, the shaped lubricant compound products thus
obtained having at least one reproducibly controlled dimension. The method may be
carried out using a variety of equipment such as screw extruders, roller extrusion
presses, or roller presses. The grinding action which occurs in pellet production
on pellet presses, whether on stationary dies with rotating roller pressure or rotating
dies with stationary roller pressure, effectively reduces agglomerates resulting in
a more uniform wire drawing compound product which in turn results in more uniform
coating on the wire.
[0028] The dry wire drawing lubricant compounds useful in this invention have been widely
described in the literature such as the following, each of which is incorporated herein
by reference. One such publication, an article by Richard Platt titled "Choosing a
Powdered Lubricant for Ferrous Wire Drawing" in Wire Technology, May 1989, discusses
the general composition of dry wire drawing lubricant and provides a table of properties
relating the composition to residual film thickness. Another article titled "Lubrication
of Ferrous Wire" in Ferrous Wire, Volume 1, "The Manufacture of Ferrous Wire," published
by the Wire Association International, Inc., discusses various types of lubricants,
their proper selection, and some of the terminology - thus, the industry accepted
terms descriptive of the lubricants which leave a thick residual film on the wire
is "lean," while those leaving a thin film are referred to as "rich." The "rich" lubricants
are higher in fatty acid content than the "lean" lubricants. A further classification
discussed by Platt divides the dry wire drawing compounds into soluble sodium soap
compounds and insoluble calcium soap compounds. A "lean" soap formulation typically
contains 30% fatty acid while a "rich" soap formulation typically contains 70% fatty
acid. Both of these articles disclose that other additives may be present to help
maintain viscosity during the drawing process, to act as extreme pressure lubricants,
to provide anti-corrosion characteristics, and to add color. U.S. Patent No. 2,956,017
(Franks) discloses calcium soap compositions useful in dry wire drawing compounds.
Franks further notes that combination of the calcium soaps with diamide waxes is beneficial.
U.S. Patent No. 4,404,828 (Blatchford) discusses the wire drawing process utilizing
dry wire drawing lubricant powders, the classification and composition of dry wire
drawing powdered lubricants, the dust problem associated with powdered lubricants,
and so on.
[0029] The dry wire drawing lubricant compounds useful with the present invention are those
which are based on metal soaps, particularly calcium soaps and sodium soaps as described
in the aforementioned references. The process described herein is also beneficial
in the reprocessing of "spent" wire drawing compounds - that is, those materials which
have been rejected by the die system or have passed through the die or dies and have
become separated from the wire. They may be unchanged in chemical composition or modified
by heat exposure, metal pick up or other forms of contamination. Such materials are
frequently in the form of scales or flakes, string like materials or powder. These
spent materials may be recovered by vacuum systems, for example, and reprocessed alone
or blended with virgin wire drawing compound to produce satisfactory shaped constructions
of dry wire drawing compounds, frequently without intermediate purification steps.
[0030] The method of the invention comprises the steps of (A) conglutinating the dry wire
drawing lubricant composition and (B) shaping the conglutinated product under controlled
pressure to provide a dust-free shaped lubricant product having at least one reproducibly
controlled dimension, pulverizable by the wire drawing process. Steps A and B can
be carried out sequentially or simultaneouly.
[0031] "Conglutination" is a term used to describe the process of sticking together a mass
of individual particles as though glued together. The conglutinating "agent" is a
combination of heat and pressure, with or without water being present. If water is
present, it may be water remaining in the metal soap composition generated during
the reaction of the metal hydroxide with the fatty acid or it may be added to the
process, for example, at the pressure forming step. If water is present it will normally
be present in the range of from about 0.5 to about 10.0 weight percent of the finished
product weight. The maximum water present in any given composition of wire drawing
compound is dependent on the end use of the wire drawing compound and varies with
the wire composition, process configuration, and wire speed.
[0032] Elevated temperatures may be employed to facilitate conglutination and pressure forming
to the desired shape and physical strength of the finished product. Elevated temperatures
used in the process will be below the melt point of the metal soap used in the dry
wire drawing lubricant. Preferred temperatures range from about 50 to about 120 degrees
Centigrade, most preferably 70-90. These elevated temperatures refer to the temperature
of the dry wire drawing compound composition as it enters the forming equipment or
present in the forming equipment. The elevated temperatures of the lubricant composition
may be residual heat from the soap forming step or may be added by exposing the composition
to elevated temperatures or by supplying heat to those portions of the forming equipment
which contact the dry wire drawing compound during forming. Where the pressure forming
equipment comprises a portion of a continuous process, the residual heat of the soap
production is used beneficially. Pellets exiting the die plate may be advantageously
cooled by passing air across them to lower their temperature and minimize sticking
to each other or to surfaces of the process equipment. These exiting pellets may also
be subjected to a vacuum, at or close to the cutter bar which cuts the pellets to
the desired length, in order to reduce or eliminate fine particles which may be generated
during the cutting or breaking action.
[0033] The pressure to be applied to the conglutinated or conglutinating product to form
the shaped, dust-free dry wire drawing compound covers a wide range and is determined
by the metal soap composition of the dry wire drawing compound, the strength required
for the shaped articles to withstand the rigors of shipping and handling and still
be useful in wire drawing, and the process forming equipment being used. It is also
influenced by the temperature being employed and by the presence or absence of water.
It is the physical strength required of the final shaped product which determines
how much pressure is to be used. For example, pellets (or other constructions) of
dry wire drawing compound produced by the process of this invention should be strong
enough to resist breakage or deterioration to powder during shipping and handling
(generally able to withstand pressures of at least about 10 pounds per square inch)
but pulverize readily when in contact with the moving wire (generally satisfactory
if pulverizable at a pressure below about 300 pounds per square inch). It is essential
that such pellets be reduced in size rapidly during the wire drawing operation in
order that they can enter the approach zone of the die where softening and melting
to a plastic film begins. Some pellets, particularly those below 1 mm diameter, can
enter the approach zone or go directly into the melt without pulverizing.
[0034] While the action of the wire moving through the pellets in the soap box is the primary
force which pulverizes the pellets, it may be desirable at initial startup of a wire
drawing line to add a small amount of pulverized wire drawing compound to the soap
box to insure complete coating of the wire prior to the pulverization process reaching
equilibrium. Another means of accomplishing this is to use lubricant applicators which
are well known in the art for breaking up lubricants and forcing the powder onto the
wire.
[0035] A particular advantage of the shaped constructions of wire drawing compounds described
herein is that they form a "blanket" over pulverized material in the soap box. The
larger shaped constructions rise to the top of the soap box while the pulverized materials
remain at the bottom of the soap box surrounding the wire. This blanketing action
suppresses the release of finely pulverized wire drawing compound to the atmosphere.
A further advantage of these shaped constructions is that the coatings deposited on
the wire are more uniform than those produced using conventional powdered wire drawing
compounds, possibly due to segregation of powdered material into non-homogeneous layers
during shipping and handling; the uniformly coated wire in turn is easier to process
in post drawing operations.
[0036] The shaped dust-free wire drawing lubricants produced by the inventive process may
be produced in a wide variety of shapes, such as cubes, balls, cylinders, pellets,
or flakes. It is, however, essential that at least one dimension be reproducibly controlled
and not be so large as to be unusable in the wire drawing operation. In general, large
diameter wire can be processed with large or small constructions of shaped wire drawing
lubricants produced by the inventive process, while small diameter wire will normally
require smaller constructions of wire drawing compounds. A typical size for products
of this invention which can be used successfully in wire drawing is one having a diameter
or thickness of from about 0.5 to about 10 mm. All other dimensions will be approximately
5-7 times the controlled dimension, or less.
[0037] The indication that the lubricant constructions have at least one reproducibly controlled
dimensions includes the use of a blend of two or more sets of pellets, each set of
pellets varying in the size of the reproducibly controlled dimension(s).
[0038] A preferred shape of the product is a cylindrical pellet having a diameter of 2 mm
and a length of no greater than 10 mm. Two most preferred embodiments are pellets
having a diameter of 1.6 mm and a length of approximately 10 mm and pellets having
a diameter of 1 mm and a length of approximately 5 mm.
[0039] Some representative examples follow:
Examples A-D:
[0040] Representative dry wire drawing lubricants were prepared in a stirred reactor to
a final temperature of 90 degrees Centigrade and formed into dust-free pellets on
a roller extrusion press. The compositions are shown in the following Table I.
[0041] The roller extrusion press used in the experiment comprised a flat die plate having
a plurality of 1 mm diameter perforations 3 mm in length. A series of two rollers
moved transversely across the top openings of each of the perforations every 2 to
3 seconds. The rollers were suspended approximately 0.75 mm above the top surface
of the die plates. The lubricant compositions of examples A through D were fed continuously
into the space between the roller surface and the die plate. The lubricant composition
was converted from essentially powder to continuous extruded strands through each
die plate perforation. A breaker blade, rotating below the die plate and adjusted
for distance from the die plate and speed of rotation controlled the length of each
generated pellet. Thus, the extruded strands, 1 mm in diameter, were cut or chopped
to a controlled length of approximately 7 mm average.
[0042] The water reported in Table I is used in the formulation to convert the metal oxides
to metal hydroxides which in turn react with the fatty acids to form soaps. The additives
are conventional fillers, thickeners, anti-corrosives, and the like.
TABLE I
DRY WIRE DRAWING SOAP COMPOSITION |
|
Soluble Sodium Soaps (weight %): |
Insoluble Calcium Soaps (weight %): |
|
Rich |
Lean |
Rich |
Lean |
Example |
A |
B |
C |
D |
Fatty Acid |
72 |
49 |
58 |
32 |
Metal Oxide |
9 |
5.5 |
30 |
50 |
Additives |
13 |
39.5 |
2 |
3 |
Water |
6 |
6 |
10 |
15 |
[0043] It was found that the pelletized dust-free pulverizable dry wire drawing compounds
of examples A through D could be pulverized back to powder by applying a force of
approximately 20 pounds per square inch (psi). The pellets of examples A through D
were sufficiently cohesive to resist breakage during packaging and shipping.
[0044] Evaluation of the pellets of examples A and C were carried out on production size
wire drawing equipment. The results are shown in Table II. The "Controls" were the
same lubricant compositions but in unpelletized form. With the insoluble calcium soap
(example C), an additional 10 weight percent water was added at the pressure forming
stage to produce pellets containing approximately 5 weight percent unreacted water
after partial drying.

Examples E-F:
[0045] A test was run to determine applicability of the process to reprocessing of "spent"
material. Following some wire drawing operations, spent lubricant (a rich, soluble,
sodium soap) was collected from the floor under the wire drawing machine and from
the soap box, care being taken to exclude metal particles and non-soap products. The
spent material was dusty and had an analysis similar to that of Example A above, except
that the fatty acid content was about 77%, the metal oxides about 15%, the additives
about 8%, and the water less than 1%. This material was repelletized on a 1mm die,
some as is (Example E) and some (Example F) mixed with virgin material (75% spent/25%
virgin), the virgin material being about 79-81% fatty acid, about 10-13% metal oxide,
about 4-6% additives, and less than 2% water. Pellets made from both materials showed
positive lubrication results in a one hour evaluation.
Example G:
[0046] A series of evaluations were made to determine the strength of pellets produced according
to this invention, "strength" referring to resistance to pulverization to powder where
exposed to pressure between opposing platens in a machine (an Instron 4204 Tester)
designed to evaluate physical properties of dry materials. The tests were run on pellets
made from various rich and lean, sodium and calcium based, compositions, with diameters
varying from 0.8 to 6.2 mm and lengths varying from 3.4 to 13.3 mm. The results in
all cases showed that the pellets were resistant to pulverization at pressures below
about 17 psi and were readily pulverized at pressures between about 17 psi and about
292 psi.
1. Shaped, dust-free dry wire drawing lubricants which are comprised of metal soaps,
have at least one reproducibly controlled dimension, and are pulverizable by wire
drawing processes into viscous lubricating films.
2. A shaped lubricant as in Claim 1 which is in the form of a cylindrical pellet.
3. A shaped lubricant as in Claim 2 wherein the pellet resists breakage at a force of
about 10 psi.
4. A shaped lubricant as in Claim 2 wherein the pellet pulverizes readily at a force
between about 10 psi and about 300 psi.
5. A shaped lubricant as in Claim 2 wherein the pellet has a diameter of 1 to 2 mm and
an average length of 5 to 10 mm.
6. A shaped lubricant as in Claim 1 wherein the lubricant contains a sodium or calcium
soap.
7. A method of providing wire with a uniform coating of lubricant during wire drawing
which comprises pulling said wire, prior to drawing, continuously through a bed containing
the shaped, dry wire drawing lubricant of Claim 1.
8. The coated wire of Claim 7.
9. A method as in Claim 7 wherein some of the lubricant in the bed is in pulverized form.
10. A method of making shaped, dust-free dry wire drawing compounds which are comprised
of metal soaps, have at least one reproducibly controlled dimension, and are pulverizable
by wire drawing processes into viscous lubricating films, which method comprises conglutinating
and shaping the dry wire compound composition under controlled pressure.
11. A method as in Claim 10 wherein the composition contains a sodium or calcium soap.
12. The method of Claim 10 conducted in the presence of water.
13. A method as in Claim 10 wherein the composition is conglutinated at a temperature
of from about 50 to about 120 degrees Centigrade.
14. A method as in Claim 10 wherein a roller extrusion press is employed to do the shaping.
15. A method as in Claim 10 wherein the composition is comprised of spent wire drawing
compounds.