US2056426A - Magnetic separation method and means - Google Patents

Magnetic separation method and means Download PDF

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US2056426A
US2056426A US614380A US61438032A US2056426A US 2056426 A US2056426 A US 2056426A US 614380 A US614380 A US 614380A US 61438032 A US61438032 A US 61438032A US 2056426 A US2056426 A US 2056426A
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Frantz Samuel Gibson
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03CMAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
    • B03C1/00Magnetic separation
    • B03C1/02Magnetic separation acting directly on the substance being separated
    • B03C1/035Open gradient magnetic separators, i.e. separators in which the gap is unobstructed, characterised by the configuration of the gap

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  • the pu p of y invention is 190' provide a comparison with other-separators, so that the magnetic separator to separate mixtures of varilength of the action of the magnetic force on the one minerals into their component constituents grain is relatively long, both in space and in time, on the basis of their magnetic susceptibilities. and especially if the operating space is filled with In particular my invention provides a more ecowater.
  • my invention provides a more ecowater.
  • the magnetic force may magnetic particles in the grain mixture by means be made substantially a constant for any particle, of localized concentrations of magnetic flux; that is, independent of the position of the particle 1:, typical of such arrangements are the field bein the operating space, so that the direction of K5 tween a pointed and a flat pole piece, and the motion assumed by particles in that space will be field near a magnetized serrated or laminated practically independent or the initial positions rotor or other attractor.
  • the operating space is -a small orthe less magnetic fraction is determined only volume immediately surrounding a line parallel partly by its mass susceptibility, and quite largeto the rotor axis and passing through the point ly also by the fortuitous circumstance of the where the grain stream leaves the rotor. Also, in position and velocity of the particle at its enthe old Edison machine the grain is dropped trance into the operating space.
  • Fig. 1 is a longitudinal cross section of a separator embodying my invention, taken on the line C--C of Fig. 2.
  • Fig. 2 is a cross section on the line A-A o'i" Fig. 1.
  • Fig. 3 is a side view of the separator shown in Fig. 1 as seen from the direction of the arrow B.
  • Figs. 4 and 5 are schematic views showing a Figs. 9 to 12 inclusive are diagrams to illustrate the motions of particles in various kinds of magnetic fields.
  • Fig. 13 is a schematic representation in cross section of the magnetic circuit of a separator.
  • Figs. 1 to 3 inclusive I have indicated at 9 inclined tubes into which the mixture to be separated is introduced from the hopper III by feed pipe I l.
  • Each tube 9 is placed between pole pieces i 2 whose surfaces adjacent the tube 8 are shaped soas to provide within the tube a magnetic field of suitable configuration which will be discussed later.
  • the windings I 3 energized from some suitable source of electricity serve to supply magneto-motive force across the gaps between the pole pieces I 2.
  • Near the lower termination of the pole pieces l3 there is placed within each tube a divider H which serves to keep apart the products of the separation and to allow them'to be conveyed into separate receptacles l5 and I6 through the discharge tubes l1 and I8 respectively.
  • the device may either be operated flooded with water as shown, or it may be operated dry; in the latter case the grain being dried sufficiently so that the particles do not adhere to one another.
  • the operation of the device wet will now be described.
  • the grain mixture fed through I l' into hopper III descends through the tubes 9; Upon :a-rriving'adjacent to the upper extremity of the pole pieces the particlesfind themselves in a magnetic field which tends to urge the more magnetic constituents in the direction upwards and towards the right in Fig. 1.-
  • the dots l9 sink downwards under the influence of gravity. The less magnetic particles 20 continue to slide down the lower or outer part of the tube 9 undisturbed bythe magnetic field.
  • turbulence in the water of the upper part of tube 9, in order that all the particles may be freed from each other to prevent entrainment of non-magnetic particles with the stream it or of magnetic particles with the stream 20.
  • This turbulence may be achieved by the use of water jets, mechanical stirrers or the like. In many cases. however, such devices are wholly unnecessary.
  • FIG. 4 A modification of the type of separator shown in Fig. 1 is illustrated in Figs. 4 and 5.
  • the space between the pole faces I 2 contains a horizontal trough 2
  • the grain is fed through a'pipe Ii andfails to the bottom of the trough.”
  • I is a screw conveyor-s23 suitably driven to propel the grain to the right in Fig. 5.
  • the grain reaches the operatingspace between the pole faces II the more magnetic constituents are'liftedby the mag-' netic force and riseto the surface of thewater;
  • a conveyor is provided which moves these more magnetic grains to the divider along the surface of the water.
  • the divider l4 serves to keep the two constituents separated as they emerge from the operating space.
  • a detail of practical importance in either form is the configuration of the pole faces 12 near the discharge end. Instead of being cut ofi squarely, as they may be at the feed end, they should be cut away according to a curve somewhat resembling that shown in Fig. 6 at l2. The purpose of this curvature is to prevent the clogging of the machine by "an unduly great convergence of magnetic field tending to hold magnetic particles at the ends of the pole faces nearest the discharge.
  • Fig. '7 shows another arrangement embodying my invention.
  • the pole faces are designated at l2. Between these faces there are any number of operating spaces 9 which may be tubes as -irr-Figi 2.
  • the winding l3 serving to energize the device.
  • the operating-spaces 9 as well as the pole faces I! are preferably of hellcoidal form, so that particles descending through 9 will at the same time undergo a rota motion about the axis.
  • Splitters l4 placed in the spaces S-near the bottom of the device serve to separate the magnetic from the non-magnetic particles.
  • the magnetic particles are drawn in by magnetic forces towards the axis; the less magnetic particles are kept toward the outside in their descent by the centrifugal force resulting from their rotary motion.
  • Suitable means are provided for feeding each space 9 at the top near the periphery and for discharging the separation products at the bottom.
  • the winding It may be closed externally through another similar device set beside the first one, if desired.
  • operating space space, zone or volume in a magnetic separator in which magnetic forces are applied to the particles to give physical separation on the basis of the magnetic susceptibilities of the particles.
  • cylindrical force field is meant a magnetic field in which surfaces representing equal magnitudes of H are cylindrical surfaces (not necessarily of revolution).
  • direction of the axis of a cylindrical force field is meant the direction of the elements of these cylinders.
  • isodynamic magnetic field a magnetic field in which the gradient of meant a magnetic field in which the gradient ofthe square of the field intensity decreases in magnitude in the direction in which the square of the magnetic field intensity increases.
  • katadynamic magnetic field is meant a magnetic field in which the gradient of the square of the field intensity increases in magnitude in the direction in which the square of the magnetic field intensity increases.
  • isodynamic magnetic separator a magnetic separator in which throughout a considerable part of the operating space the magnetic field is substantially isodynamic.
  • anadynamic magnetic separator a magnetic separator in which throughout a. considerable part of the operating space the magnetic field is anadynamic.
  • Fig. 9 represents a particle in a katadynamic magnetic field such as is found in all previous magnetic separators of which I am aware. Assume a magnetic particle to be placed at c and the magneto motive force adjusted so that the magnetic force on the particle is just equal and opposite to its weight. If now the particle be moved ever so little above the point e, the magnetic force will exceed the weight of the particle and the particle will be drawn upward with ever-increasing acceleration until it strikes the upper pole piece at d. If the particle be moved downward ever so little from c, the magnetic force will become insufficient to sustain it and the particle will drop downward by gravity until it strikes the lower pole piece at 12. Hence the motion of a particle of given susceptibility upward or downward is determined by the initial position and velocity which it may happen to have in the operating space.
  • Fig. 10 also shows a katadynamic field arrangement with differently shaped pole pieces.
  • the remarks above as to Fig. 9 apply equally to Fig. 10.
  • Fig. 11 represents a particle in an lsodynamic magnetic field. Assume a particle of a certain definite'susceptibility to be placed at point and the magneto motive force of the magnet adjusted so that the magnetic force on the par ticle is just equal and opposite to its weight.
  • Fig. 12 illustrates the behavior of a magnetic particle in an anadynamic field. Assume a par ticle of a certain definite susceptibility be placed at point e" and the magnetomotive force adjusted so that the magnetic force is just equal and opposite to the gravitational force. If now the particle be displaced upward and released it will return to point above which the gravitational force exceeds the magnetic force for this particle, and below which the magnetic force upward exceeds the gravitational force. Therefore 0" is the position of equilibrium for this and similar particles on the line of symmetry.
  • a particle of greater susceptibility than the first be placed at c" and released it will move upward to some such position as d" at which it would be in stable equilibrium as regards vertical forces, and to which it would return if displaced either up or down from d".
  • a particle of less susceptibility would likewise find a position of stable equilibrium at some such point as b".
  • all particles of the same susceptibility will tend to be in equilibrium as regards vertical forces at the same height, and if a mixture of particles of different susceptibilities be introduced into the field the particles will tend to arrange themselves in horizontal layers at heights corresponding to their susceptibilities.
  • Fig. 13 which is a schematic representation in cross section of the magnetic circuit of-a separator embodying my invention
  • I is the core about which is wrapped the winding 2 supplied with electric current from a suitable source.
  • 3 and 3' are the pole pieces forming the termination of core I.
  • Their opposing surfaces 4 and 4' are shaped to a special form which is discussed below.
  • 5-5 represent the plane of symmetry of the device
  • 6-6' is a horizontal plane to which surfaces 4 and 4' are asymptotic as they are also to 5--5'.
  • I--'I and 88' are planes parallel to 6 -6' which limit approximately the operating space of the device.
  • the energy density of a magnetic field equals the energy gradient is a vector having the same direction as the gradient of H and a magnitude times as great.
  • the expressions direction of energy gradient and direction of gradient of H are therefore synonymous, and correspond to the direction in which a particle of given positive susceptibility is urged by a magnetic field.
  • cylindrical refers to a field whose equipotentials are cylindrical surfaces. It is obvious that neither such a field nor its energy gradient can have any component in the direction of the elements of the cylindrical surfaces.
  • pole pieces having cylindrical pole faces contoured substantially to the form of equipotential surfaces of a cylindrical isodynamic field, a gap between said faces, and means for feeding a grain stream through said gap and substantially parallel to the elements of said faces, whereby particles in said stream are urged in the direction of the energy gradient of said field and substantially perpendicular to said stream.
  • pole pieces having cylindrical pole faces contoured substantially to the form of the curves x y a constant.
  • pole pieces having cylindrical pole faces contoured substantially to the form of the curves x y a constant where a is not less than zero.
  • a magnetic separator in accordance with the present invention, a feed channel, and pole pieces so contoured as to produce in said channel an isodynamic field, said channel being between and substantially parallel to the faces of said pole pieces and perpendicular to the direction of the energy gradient of said field, whereby magnetic particles in said channel are urged in the direction of said energy gradient and substantially perpendicular to said channel.
  • a feed channel and pole pieces so contoured as to produce in said channel an anadynamic field, said channel being between and substantially parallel to the faces of said pole pieces and perpendicular to the direction of the energy gradient of said field, whereby magnetic particles in said channel are urged in the direction of said energy gradient and substantially perpendicular to said channel.
  • cylindrical pole pieces on either side of an elongated operating space, said pole pieces being so contoured as to produce within said operating space a field in which the gradient of H is substantially constant in magnitude and feed means for feeding a grain stream through said operating space in the direction of its length, whereby magnetic particles in said stream are urged in a direction substantially perpendicular to said stream.
  • pole pieces so shaped as to give in the operating space between them a force on a magnetic particle which remains substantially constant as the particle moves in the direction of said force in said space and means for feeding particles through said space in a direction substantially perpendicular to said force and parallel to the faces of said pole pieces.
  • Magnetic separator comprising a feed tube inclined from the vertical, means for feeding grain and water into the upper end of said tube, two elongated convex cylindrical pole pieces on opposite sides of said tube and parallel with said tube effective to urge magnetic particles toward one side of said tube, and constricted discharge means at the bottom of said tube.
  • Magnetic separator as claimed in claim 8 in which the pole pieces are contoured substantially to the form of equipotential surfaces of a cylindrical isodynamic field.
  • Magnetic separator comprising two elongated horizontal cylindrical pole pieces, a horizontal trough disposed between said pole pieces, means for feeding grain into one end of said trough, conveying means for conveying the grain towards the other end of said trough, said pole pieces being contoured substantially to the form of equipotential surfaces of a cylindrical isodynamic field, the direction of the energy gradient of said field being substantially perpendicular to the direction of fiow of grain through said trough.
  • Magnetic separator comprising a helical channel disposed around a vertical axis, feed means for feeding a grain stream thereinto, and pole pieces having continuous pole faces respectively above and below said channel, the gap between said pole faces decreasing with decreasing radius from the axis, whereby to exert inward radial forces on magnetic particles in said chanhe].
  • Magnetic separator as claimed in claim 11, in which the gap between said pole faces decreases less rapidly with decreasing radius than the gap given by the formula xNR-r) a constant, where a: is the gap, 1' the radius from the axis and R. a constant, whereby to give an anadynamic field.
  • cylindrical pole pieces on either side of an elongated operating space, said pole pieces being so contoured as to produce within said operating space a field in which the gradient at H is substantially constant in magnitude, and feed means for feeding a grain stream through said operating space in the direction of its length, whereby magnetic particles in said stream are urged in a direction substantially perpendicular to said stream, said pole pieces at their discharge ends being so flared as to produce a gradually decreasing field in the space between them, whereby the discharge of magnetic particles is facilitated.

Description

Oct 6, 1936. s, NT I 2,056,426
MAGNETIC $EPARATION METHOD AND MEANS Original Filed May 31, 1932 5 Sheecs-Sheet 1 11160616201 fimmael 611 1201222 Oct. 6, 1936. s. G. FRANTZ MAGNETIC? SEPARATION METHOD AND MEANS Original Filed May 51, 1932 5 Sheets-Sheet 2 Oct. 6, 1936. v s FRANTZ 2,056,426
MAGNETIC SEPARATION METHOD AND MEANS Original Filed May 31, 1932 5 Sheets-Sheet 3 llllflllll K: N I 12112612101- jallzzlelal'raldz Oct. 6, 1936.
A s. e. FRANTZ MAGNETIC SEPARATION METHOD AND MEANS Original Filed May 31, 1932 5 Sheets-Sheet 4 lit/$118121- Oct, 6, 19369 s FRANTZ 2,056,426
r MAGNETIC SEPARATION METHOD AND. MEANS Original Filed May 51, 1932 5 Sheeis-Sheet 5 I nyw fiiveutor ,iamuel G-flaatz Patented Oct. 6, 1936 2,056,426
UNITED STATES PATENT OFFICE MAGNETIC SEPARATION METHOD AND MEANS Samuel Gibson Frantz, Princeton, N. J.
Application May 31, 1932, Serial No. 614,380 Renewed February 5, 1936 19 Claims. 209-232) The pu p of y invention is 190' provide a comparison with other-separators, so that the magnetic separator to separate mixtures of varilength of the action of the magnetic force on the one minerals into their component constituents grain is relatively long, both in space and in time, on the basis of their magnetic susceptibilities. and especially if the operating space is filled with In particular my invention provides a more ecowater. Thus it is that in my invention the mag- 6 nomical and more precise method of separating netic force on a particle instead of being of such certain kinds of mixtures than do the devices short duration as to be considered an impulse, heretofore used. The various other advantages is in general of such long duration that the diwill be apparent from the specification which foirection of motion assumed by a particle is sublows. stantially the direction of the resultant of the it) In general in magnetic separators heretofore magnetic and gravitational forces on the particle. used, magnetic forces have been exerted on the Also, as will be shown the magnetic force may magnetic particles in the grain mixture by means be made substantially a constant for any particle, of localized concentrations of magnetic flux; that is, independent of the position of the particle 1:, typical of such arrangements are the field bein the operating space, so that the direction of K5 tween a pointed and a flat pole piece, and the motion assumed by particles in that space will be field near a magnetized serrated or laminated practically independent or the initial positions rotor or other attractor. It seems to be inherent and velocities of the particles on their entrance in these previous designs that the operating to the space, which are irrelevant to the purpose space, that is the space in the magnetic field of the separation, but will be almost solely a 20 where magnetic forces are effective to cause sepfunction of the mass susceptibility of the particle. aration of magnetic from non-magnetic particles, In all previous magnetic separators, so far as is very much restricted in volume. Thus for ex- I am aware, the-question of whether a given parample, in a rotor type machine as shown by Johnticle will be discharged with the more magnetic son and others, the operating space is -a small orthe less magnetic fraction is determined only volume immediately surrounding a line parallel partly by its mass susceptibility, and quite largeto the rotor axis and passing through the point ly also by the fortuitous circumstance of the where the grain stream leaves the rotor. Also, in position and velocity of the particle at its enthe old Edison machine the grain is dropped trance into the operating space. This is so beso through a columnar space in which the operating cause in those separators the effective magnetic spaces are small spaces adjacent to the pole pieces force to cause separation is not the same for vaof the magnets, and the rest of the columnar rious paths through the operating space, but is space is not usefully employed for separation. different for different paths and may vary several It is obvious that since every particle must be hundred percent between different possibl p s passed through the operating space, for a given of a particle.
rate of feed for the grain the time during which An example may serve to make clear the ima particle is in the operating space will be very portance of this. Supposea magnetic separasmall if the operating space is small. It follows tor of any type previously used is fed with a. mixthat ifthe volume which is efiective as operating ture of equal parts of grains A and B, B having 40 space is greatly increased, either the tonnage caa mass susceptibility of 10- and A a mass sus- 40 pacity or the sensitiveness of the machine 'will. ceptibility twice as great, or 2 l0 and suppose be correspondingly increased; for if the same the current in the winding to be adjusted so that tonnage were fed through the larger operating half of the total feed is delivered in each of the space the time during which magnetic forces act fractions discharged by the separator, X and Y.
on a given particle would be greater. If a perfect separation had been made all the 45 My invention relates to separating machines A grains would go into fraction X, and all the B in which the operating space is a large volume grains into Y. Previously used separators howas compared with the localized and restricted ever will not approach a perfect separation beoperating spaces of the previously used separatween grains whose susceptibilities are so close tors, and particularly to machines in which the together, and it will be found that X is composed 50 magnetic field in the operating space is of a speof say 65% A and 35% B, and Y of 65% B and cial configuration. 35% A. The reason is that although the mean In separators embodying my invention the magnetic force for all paths is just sufficient to length of the operating space, measured parallel I remove particles of mass susceptibility greater to the flow of the grain is in general great in than l.5 10- and to reject those at lower mass susceptibility, on some paths the effective force is perhaps three times as strong, and all particles having such paths will be delivered to fraction X regardless of whether they are A or B. Similarly certain other paths followed by some of the particles are through regions in which the effective force due to the field is perhaps only half as great as the mean, and insufllcient to remove either A or B, which are both indiscriminately passed to fraction Y.
Thus it is seen that to make a good separation between two components whose mass susceptibilities are close together it is important that the effective magnetic force on a particle for different paths shall be substantially a constant. Previously used separators have not been able nor so far as I am aware tried so to control the configuration of the m netic field that its effect on a particle is independent of its initial path. This control is one of the objects of the present invention.
Other advantages will be apparent from the specification which follows.
In the drawings:
Fig. 1 is a longitudinal cross section of a separator embodying my invention, taken on the line C--C of Fig. 2.
Fig. 2 is a cross section on the line A-A o'i" Fig. 1.
Fig. 3 is a side view of the separator shown in Fig. 1 as seen from the direction of the arrow B.
Figs. 4 and 5 are schematic views showing a Figs. 9 to 12 inclusive are diagrams to illustrate the motions of particles in various kinds of magnetic fields.
Fig. 13 is a schematic representation in cross section of the magnetic circuit of a separator.
In Figs. 1 to 3 inclusive, I have indicated at 9 inclined tubes into which the mixture to be separated is introduced from the hopper III by feed pipe I l. Each tube 9 is placed between pole pieces i 2 whose surfaces adjacent the tube 8 are shaped soas to provide within the tube a magnetic field of suitable configuration which will be discussed later. The windings I 3 energized from some suitable source of electricity serve to supply magneto-motive force across the gaps between the pole pieces I 2. Near the lower termination of the pole pieces l3 there is placed within each tube a divider H which serves to keep apart the products of the separation and to allow them'to be conveyed into separate receptacles l5 and I6 through the discharge tubes l1 and I8 respectively.
The device may either be operated flooded with water as shown, or it may be operated dry; in the latter case the grain being dried sufficiently so that the particles do not adhere to one another. The operation of the device wet will now be described. The grain mixture, fed through I l' into hopper III descends through the tubes 9; Upon :a-rriving'adjacent to the upper extremity of the pole pieces the particlesfind themselves in a magnetic field which tends to urge the more magnetic constituents in the direction upwards and towards the right in Fig. 1.- The dots l9 sink downwards under the influence of gravity. The less magnetic particles 20 continue to slide down the lower or outer part of the tube 9 undisturbed bythe magnetic field. In some cases it may be desirable to promote turbulence in the water of the upper part of tube 9, in order that all the particles may be freed from each other to prevent entrainment of non-magnetic particles with the stream it or of magnetic particles with the stream 20. This turbulence may be achieved by the use of water jets, mechanical stirrers or the like. In many cases. however, such devices are wholly unnecessary.
The more magnetic particles move downward and pass above the divider it before they pass out\ of the magnetic field which terminates near the lower ends of the pole pieces I2. They are then discharged through the pipe it into a suitable receptacle IB. The less magnetic particles pass below the divider II and are discharged through thepipe "l1 into ll.
A modification of the type of separator shown in Fig. 1 is illustrated in Figs. 4 and 5. In Fig. 4 the space between the pole faces I 2 contains a horizontal trough 2|. This trough is filled with water up to the level 22. The grain is fed through a'pipe Ii andfails to the bottom of the trough." In the bottom of the trough 2 I is a screw conveyor-s23 suitably driven to propel the grain to the right in Fig. 5. *When'the grain reaches the operatingspace between the pole faces II the more magnetic constituents are'liftedby the mag-' netic force and riseto the surface of thewater;
A conveyor is provided which moves these more magnetic grains to the divider along the surface of the water. The divider l4 serves to keep the two constituents separated as they emerge from the operating space. A detail of practicalimportance in either form is the configuration of the pole faces 12 near the discharge end. Instead of being cut ofi squarely, as they may be at the feed end, they should be cut away according to a curve somewhat resembling that shown in Fig. 6 at l2. The purpose of this curvature is to prevent the clogging of the machine by "an unduly great convergence of magnetic field tending to hold magnetic particles at the ends of the pole faces nearest the discharge.
It will be understood that although the embodiments of the device shown in Figs. 1 to 6 are shown as operated wet, it is also possible to operate these devices dry. In the case of Fig. 4 the conveyors 23 and 24 may then be omitted and a closed tube substituted for the troughll, and
the motion of the particles through the device assured by a shaking motion of the tube possibly supplemented by an inclination of the device in direction'ofthe fiow of grain.
Fig. '7 shows another arrangement embodying my invention. In Fig. 7 the pole faces are designated at l2. Between these faces there are any number of operating spaces 9 which may be tubes as -irr-Figi 2. Immediately surrounding the axis, which is vertical, is the winding l3 serving to energize the device. The operating-spaces 9 as well as the pole faces I! are preferably of hellcoidal form, so that particles descending through 9 will at the same time undergo a rota motion about the axis. Splitters l4 placed in the spaces S-near the bottom of the device serve to separate the magnetic from the non-magnetic particles. The magnetic particles are drawn in by magnetic forces towards the axis; the less magnetic particles are kept toward the outside in their descent by the centrifugal force resulting from their rotary motion. Suitable means are provided for feeding each space 9 at the top near the periphery and for discharging the separation products at the bottom. The winding It may be closed externally through another similar device set beside the first one, if desired.
It is well known that the force exerted by a magnetic field on a particle magnetized by induction is proportional to the gradient of the quantity H where H is the field intensity, susceptibility being considered constant; and so far as I am aware in all previously used magnetic separators the force exerted on a particle increases rapidly as the particle travels in the field under the influence of magnetic forces. In these cases, therefore, a magnetic particle is always in unstable equilibrium under the influence of magnetic and gravitational forces as-regards all possible paths of motion. This kind of field is hereinafter referred to as a katadynamic field.
For reasons both of economy and of accuracy in separation and in particular in the type of separator represented by my invention it is much more desirable that a particle of a given kind while in the separating zone of a magnetic separator should be subjected to magnetic forces which either are substantially constant regardless of the particular position of the particle in the zone, or decrease as the particle moves under the influence of the magnetic force, so that if each particle is also acted on by some constant force such as gravity, it will be in either neiitral or stable equilibrium as regards motion along the line of the gradient of H. I shall now disclose out the separating space the magnitude of the gradient of the square of the field strength is either sumtantially a constant, or decreases as the value of H increases. are hereinafter referred to, respectively, as isodynamic and anadynamic.
By the term "operating space" is meant that space, zone or volume in a magnetic separator in which magnetic forces are applied to the particles to give physical separation on the basis of the magnetic susceptibilities of the particles. ,7
By the term cylindrical force field" is meant a magnetic field in which surfaces representing equal magnitudes of H are cylindrical surfaces (not necessarily of revolution). By the term "direction of the axis of a cylindrical force field" is meant the direction of the elements of these cylinders.
In other words, in a cylindrical force field corresponding points in different cross sections taken perpendicular to the axis have the same values of H.
By the term isodynamic magnetic field is meant a magnetic field in which the gradient of meant a magnetic field in which the gradient ofthe square of the field intensity decreases in magnitude in the direction in which the square of the magnetic field intensity increases.
By the term katadynamic magnetic field" is meant a magnetic field in which the gradient of the square of the field intensity increases in magnitude in the direction in which the square of the magnetic field intensity increases.
These kinds of field.
By the term isodynamic magnetic separator is meant a magnetic separator in which throughout a considerable part of the operating space the magnetic field is substantially isodynamic.
By the term anadynamic magnetic separator is meant a magnetic separator in which throughout a. considerable part of the operating space the magnetic field is anadynamic.
which is the gradient of H The derivative of this gradient with respect to y is ar and at any point a being a function of position.
\ For an isodynamic field, a is zero.
For an anadynamic field, a is finite and real.
For a katadynamic field, a. is imaginary.
In accordance with these definitions, it will be seen that the previously used magnetic separators, as pointed out above, are katadynamic.
I have illustrated in Figs. 9 to 12 inclusive the difference in the behavior of particles in the three kinds of fields above defined.-
Fig. 9 represents a particle in a katadynamic magnetic field such as is found in all previous magnetic separators of which I am aware. Assume a magnetic particle to be placed at c and the magneto motive force adjusted so that the magnetic force on the particle is just equal and opposite to its weight. If now the particle be moved ever so little above the point e, the magnetic force will exceed the weight of the particle and the particle will be drawn upward with ever-increasing acceleration until it strikes the upper pole piece at d. If the particle be moved downward ever so little from c, the magnetic force will become insufficient to sustain it and the particle will drop downward by gravity until it strikes the lower pole piece at 12. Hence the motion of a particle of given susceptibility upward or downward is determined by the initial position and velocity which it may happen to have in the operating space.
Fig. 10 also shows a katadynamic field arrangement with differently shaped pole pieces. The remarks above as to Fig. 9 apply equally to Fig. 10.
Fig. 11 represents a particle in an lsodynamic magnetic field. Assume a particle of a certain definite'susceptibility to be placed at point and the magneto motive force of the magnet adjusted so that the magnetic force on the par ticle is just equal and opposite to its weight.
If now the particle be moved up to point d, the magnetic force upon it will still hajust equal and opposite to its weight, and the same would be true if the particle were moved down to point I).
Fig. 12 illustrates the behavior of a magnetic particle in an anadynamic field. Assume a par ticle of a certain definite susceptibility be placed at point e" and the magnetomotive force adjusted so that the magnetic force is just equal and opposite to the gravitational force. If now the particle be displaced upward and released it will return to point above which the gravitational force exceeds the magnetic force for this particle, and below which the magnetic force upward exceeds the gravitational force. Therefore 0" is the position of equilibrium for this and similar particles on the line of symmetry.
If a particle of greater susceptibility than the first be placed at c" and released, it will move upward to some such position as d" at which it would be in stable equilibrium as regards vertical forces, and to which it would return if displaced either up or down from d". A particle of less susceptibility would likewise find a position of stable equilibrium at some such point as b". In general all particles of the same susceptibility will tend to be in equilibrium as regards vertical forces at the same height, and if a mixture of particles of different susceptibilities be introduced into the field the particles will tend to arrange themselves in horizontal layers at heights corresponding to their susceptibilities.
In Fig. 13 which is a schematic representation in cross section of the magnetic circuit of-a separator embodying my invention, I is the core about which is wrapped the winding 2 supplied with electric current from a suitable source. 3 and 3' are the pole pieces forming the termination of core I. Their opposing surfaces 4 and 4' are shaped to a special form which is discussed below. 5-5 represent the plane of symmetry of the device, 6-6' is a horizontal plane to which surfaces 4 and 4' are asymptotic as they are also to 5--5'. I--'I and 88' are planes parallel to 6 -6' which limit approximately the operating space of the device.
The mathematical expression of the shape of surfaces 4 and 4' to give between these planes 1-1 and 8-8 the best configuration of magnetic field is approximately x +t y= a constant. If a is zero, the field will be isodynamic. If a is finite and real, the field will be anadynamic. 6 is preferably small compared to unity. In other words, if the exponent of :r in the equation is equal to 2, the field is isodynamic; and if greater than 2, the field is anadynamic. If the exponent is less than 2, that is if a is imaginary the field is katadynamic. An analysis of the reasons for this is given below.
There is a certain magnetomotive force 215 available to drive the magnetic flux across the gap between 4 and 4'. In the region between I and 'I' and 8 and 8', where the surfaces 4 and 4' do not depart greatly from parallelism with 5-5, the distance travelled by the flux across the gap is substantially equal to the horizontal distance between 4 and 4; this distance will be designated by 2.1:. The distance above the plane 6-6 at which the gap is equal to 210 will be designated by 11. Then the magnetic field intensity H at any height 1 is equal to This involves the assumption, sufiiciently accurate for practical purposes, that the pole face is an equipotential surface.
Throughout this region the field gradient is substantially upward perpendicular to plane 6-6,
that is, parallel to the y axis. The field gradient therefore is equal to and the gradient of the square of the field, to which the force on a particle is proportional is dH y Since and in the isodynamic case s g =0, a constant, we may write Differentiating, we have dy c which is a constant, and therefore the force on a particle is a constant regardless of its position, within the space in which the assumptions are true.
Now if 6* is a small positive quantity it is obvious that the force will decrease as 1/ increases and the field will be anadynamic.
If 6 is negative, that is if a is imaginary the field will be katadynamic. The most useful fields are obtained when 6 is either zero or a small real quantity.
In ordinary language, it may be said that in the operating space of a katadynamic separator, a magnetic particle free to move in the direction of increasing field intensity cannot be kept in equilibrium by a constant force. On the other hand, in isodynamic and anadynamic separators, such a particle in the operating space could be maintained respectively in neutral or Stable equilibrium, as regards motion in the direction of the gradient of H, by a constant force.
Since, as is well known, the energy density of a magnetic field equals the energy gradient is a vector having the same direction as the gradient of H and a magnitude times as great. The expressions direction of energy gradient and direction of gradient of H are therefore synonymous, and correspond to the direction in which a particle of given positive susceptibility is urged by a magnetic field.
The word cylindrical is usedherein' in its broad mathematical sense of referring to surfaces generated by a straight line moving parallel to a given line and passing through a given curve. The term "cylindrical field refers to a field whose equipotentials are cylindrical surfaces. It is obvious that neither such a field nor its energy gradient can have any component in the direction of the elements of the cylindrical surfaces.
What I therefore claim and desire to secure by Letters Patent is:-
1. In a magnetic separator, pole pieces having cylindrical pole faces contoured substantially to the form of equipotential surfaces of a cylindrical isodynamic field, a gap between said faces, and means for feeding a grain stream through said gap and substantially parallel to the elements of said faces, whereby particles in said stream are urged in the direction of the energy gradient of said field and substantially perpendicular to said stream.
2. In a magnetic separator, pole pieces having cylindrical pole faces contoured substantially to the form of the curves x y=a constant.
3. In a magnetic separator, pole pieces having cylindrical pole faces contoured substantially to the form of the curves x y=a constant where a is not less than zero.
4. In. a magnetic separator, a feed channel, and pole pieces so contoured as to produce in said channel an isodynamic field, said channel being between and substantially parallel to the faces of said pole pieces and perpendicular to the direction of the energy gradient of said field, whereby magnetic particles in said channel are urged in the direction of said energy gradient and substantially perpendicular to said channel.
5. In a magnetic separator, a feed channel, and pole pieces so contoured as to produce in said channel an anadynamic field, said channel being between and substantially parallel to the faces of said pole pieces and perpendicular to the direction of the energy gradient of said field, whereby magnetic particles in said channel are urged in the direction of said energy gradient and substantially perpendicular to said channel.
6. In a magnetic separator, cylindrical pole pieces on either side of an elongated operating space, said pole pieces being so contoured as to produce within said operating space a field in which the gradient of H is substantially constant in magnitude and feed means for feeding a grain stream through said operating space in the direction of its length, whereby magnetic particles in said stream are urged in a direction substantially perpendicular to said stream.
'7. In a magnetic separator, pole pieces so shaped as to give in the operating space between them a force on a magnetic particle which remains substantially constant as the particle moves in the direction of said force in said space and means for feeding particles through said space in a direction substantially perpendicular to said force and parallel to the faces of said pole pieces.
8. Magnetic separator, comprising a feed tube inclined from the vertical, means for feeding grain and water into the upper end of said tube, two elongated convex cylindrical pole pieces on opposite sides of said tube and parallel with said tube effective to urge magnetic particles toward one side of said tube, and constricted discharge means at the bottom of said tube.
9. Magnetic separator as claimed in claim 8, in which the pole pieces are contoured substantially to the form of equipotential surfaces of a cylindrical isodynamic field.
10. Magnetic separator comprising two elongated horizontal cylindrical pole pieces, a horizontal trough disposed between said pole pieces, means for feeding grain into one end of said trough, conveying means for conveying the grain towards the other end of said trough, said pole pieces being contoured substantially to the form of equipotential surfaces of a cylindrical isodynamic field, the direction of the energy gradient of said field being substantially perpendicular to the direction of fiow of grain through said trough.
11. Magnetic separator comprising a helical channel disposed around a vertical axis, feed means for feeding a grain stream thereinto, and pole pieces having continuous pole faces respectively above and below said channel, the gap between said pole faces decreasing with decreasing radius from the axis, whereby to exert inward radial forces on magnetic particles in said chanhe].
12. Magnetic separator as claimed in claim 11, in which the pole faces are contoured substantially to the form of equipotential surfaces of an isodynamic field.
13. Magnetic separator as claimed in claim 11, in which the gap between said pole faces decreases less rapidly with decreasing radius than the gap given by the formula xNR-r) =a constant, where a: is the gap, 1' the radius from the axis and R. a constant, whereby to give an anadynamic field.
14. Magnetic separator as claimed in claim 11, in which the gap :1: between the pole faces is given substantially by the formula :c (Rr)=a con= stant, where 1' is the radius from the axis, and R is a constant, whereby to produce substantially an isodynamic field.
15. In the process of magnetic separation, that step which consists in passing the grain through an operating space in which the gradient of H is substantially constant in magnitude in a direction substantially perpendicular to the direction of said gradient.
16. In the process of magnetic separation, that step which consists in passing the grain tl'lrough an operating space between pole faces conforming substantially to equipotential surfaces of an isodynamic field in a direction substantially paral-- lel to said faces.
1'7. In the process of magnetic separation, that step which consists in passing the grain through an operating space in which the field is isodynamic in a direction substantially perpendicular to the energy gradient of said field.
18. In the process of magnetic separation, that step which consists in passing the grain through an operating space in which the field is anadynamic in a direction substantially perpendicular to the energy gradient of said field.
19. In a magnetic separator, cylindrical pole pieces on either side of an elongated operating space, said pole pieces being so contoured as to produce within said operating space a field in which the gradient at H is substantially constant in magnitude, and feed means for feeding a grain stream through said operating space in the direction of its length, whereby magnetic particles in said stream are urged in a direction substantially perpendicular to said stream, said pole pieces at their discharge ends being so flared as to produce a gradually decreasing field in the space between them, whereby the discharge of magnetic particles is facilitated.
SAMUEL GIBSON FRAN'I'L.
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Cited By (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3294237A (en) * 1963-05-31 1966-12-27 Weston David Magnetic separator
US3318447A (en) * 1964-02-03 1967-05-09 Marathon Oil Co Separation of high and low quality electrode cokes
DE1246633B (en) * 1956-01-19 1967-08-10 Robert Charles Forrer Device for the continuous magnetic separation of mineral mixtures
US3382977A (en) * 1965-03-08 1968-05-14 Interior Usa Magnetic separator with a combination field
US3474904A (en) * 1967-09-01 1969-10-28 Western Electric Co Methods and apparatus for the magnetic separation of fine parts
US3877578A (en) * 1972-09-18 1975-04-15 Occidental Petroleum Corp Separation process for flint, amber, and green glass particles from a mixture of the three colors
US4042492A (en) * 1973-04-27 1977-08-16 Klockner-Humboldt-Deutz Aktiengesellschaft Apparatus for the separation of magnetizable particles from a fine granular solid
US4062443A (en) * 1975-06-20 1977-12-13 Henry Martina System for separating ferromagnetic materials from non-ferromagnetic materials
US4102780A (en) * 1976-03-09 1978-07-25 S. G. Frantz Company, Inc. Method and apparatus for magnetic separation of particles in a fluid carrier
FR2447228A1 (en) * 1979-01-26 1980-08-22 Dn Gorny I I Electrodynamic grader for particle classification - uses criterion of density and electrical conductivity, using AC magnetic field to induce eddy currents
US4235710A (en) * 1978-07-03 1980-11-25 S. G. Frantz Company, Inc. Methods and apparatus for separating particles using a magnetic barrier
FR2567768A1 (en) * 1984-07-17 1986-01-24 Commissariat Energie Atomique ELECTROMAGNETIC FILTER WITH CONTINUOUS OPERATION
US4595494A (en) * 1983-10-05 1986-06-17 Krupp Polysius Ag Apparatus for separating ferromagnetic particles from a slurry
WO1990004458A1 (en) * 1988-10-25 1990-05-03 Elin Energieanwendung Gesellschaft M.B.H. An open-gradient magnetic separator
AT400779B (en) * 1989-07-19 1996-03-25 Gerhold Juergen Dipl Ing Dr Te Magnet system
DE19510116A1 (en) * 1995-03-21 1996-09-26 Lutz Dipl Ing Markworth Reprocessing to sort grainy to dusty material
US5568869A (en) * 1994-12-06 1996-10-29 S.G. Frantz Company, Inc. Methods and apparatus for making continuous magnetic separations
US5968820A (en) * 1997-02-26 1999-10-19 The Cleveland Clinic Foundation Method for magnetically separating cells into fractionated flow streams
US6120735A (en) * 1992-02-26 2000-09-19 The Ohio States University Fractional cell sorter
US20020090720A1 (en) * 2000-11-29 2002-07-11 Mutz Mitchell W. Focused acoustic ejection cell sorting system and method
US6467630B1 (en) 1999-09-03 2002-10-22 The Cleveland Clinic Foundation Continuous particle and molecule separation with an annular flow channel
NL2002730C2 (en) * 2009-04-08 2010-10-11 Univ Delft Tech Method and apparatus for separating a non-ferous metal-comprising fraction from ferrous scrap.
EP2267429A1 (en) 2000-12-28 2010-12-29 Picoliter Inc. Focused acoustic ejection cell sorting system and method
US20110042274A1 (en) * 2008-02-27 2011-02-24 Technische Universiteit Delft Method and Apparatus for the Separation of Solid Particles Having Different Densities
US20130015106A1 (en) * 2010-03-23 2013-01-17 Lins Guenter Device and method for magnetic separation of a fluid
US8678194B2 (en) 2009-04-09 2014-03-25 Technische Universiteit Delft Use of an apparatus for separating magnetic pieces of material
RU2561131C1 (en) * 2014-05-12 2015-08-20 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Липецкий государственный технический университет" (ЛГТУ) Magnetic divider
US11465157B2 (en) 2020-07-14 2022-10-11 Cláudio Henrique Teixeira Ribeiro Magnetic separators with stationary magnetic matrices, and methods of using the same

Cited By (37)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1246633B (en) * 1956-01-19 1967-08-10 Robert Charles Forrer Device for the continuous magnetic separation of mineral mixtures
US3294237A (en) * 1963-05-31 1966-12-27 Weston David Magnetic separator
US3318447A (en) * 1964-02-03 1967-05-09 Marathon Oil Co Separation of high and low quality electrode cokes
US3382977A (en) * 1965-03-08 1968-05-14 Interior Usa Magnetic separator with a combination field
US3474904A (en) * 1967-09-01 1969-10-28 Western Electric Co Methods and apparatus for the magnetic separation of fine parts
US3877578A (en) * 1972-09-18 1975-04-15 Occidental Petroleum Corp Separation process for flint, amber, and green glass particles from a mixture of the three colors
US4042492A (en) * 1973-04-27 1977-08-16 Klockner-Humboldt-Deutz Aktiengesellschaft Apparatus for the separation of magnetizable particles from a fine granular solid
US4062443A (en) * 1975-06-20 1977-12-13 Henry Martina System for separating ferromagnetic materials from non-ferromagnetic materials
US4102780A (en) * 1976-03-09 1978-07-25 S. G. Frantz Company, Inc. Method and apparatus for magnetic separation of particles in a fluid carrier
US4235710A (en) * 1978-07-03 1980-11-25 S. G. Frantz Company, Inc. Methods and apparatus for separating particles using a magnetic barrier
FR2447228A1 (en) * 1979-01-26 1980-08-22 Dn Gorny I I Electrodynamic grader for particle classification - uses criterion of density and electrical conductivity, using AC magnetic field to induce eddy currents
US4595494A (en) * 1983-10-05 1986-06-17 Krupp Polysius Ag Apparatus for separating ferromagnetic particles from a slurry
FR2567768A1 (en) * 1984-07-17 1986-01-24 Commissariat Energie Atomique ELECTROMAGNETIC FILTER WITH CONTINUOUS OPERATION
EP0169774A1 (en) * 1984-07-17 1986-01-29 Commissariat A L'energie Atomique Continuously functioning electromagnetic filter
WO1990004458A1 (en) * 1988-10-25 1990-05-03 Elin Energieanwendung Gesellschaft M.B.H. An open-gradient magnetic separator
AT400779B (en) * 1989-07-19 1996-03-25 Gerhold Juergen Dipl Ing Dr Te Magnet system
US6120735A (en) * 1992-02-26 2000-09-19 The Ohio States University Fractional cell sorter
US5568869A (en) * 1994-12-06 1996-10-29 S.G. Frantz Company, Inc. Methods and apparatus for making continuous magnetic separations
DE19510116A1 (en) * 1995-03-21 1996-09-26 Lutz Dipl Ing Markworth Reprocessing to sort grainy to dusty material
US5968820A (en) * 1997-02-26 1999-10-19 The Cleveland Clinic Foundation Method for magnetically separating cells into fractionated flow streams
US6467630B1 (en) 1999-09-03 2002-10-22 The Cleveland Clinic Foundation Continuous particle and molecule separation with an annular flow channel
US6849423B2 (en) 2000-11-29 2005-02-01 Picoliter Inc Focused acoustics for detection and sorting of fluid volumes
US20050130257A1 (en) * 2000-11-29 2005-06-16 Picoliter Inc. Focused acoustic ejection cell sorting system and method
US7270986B2 (en) 2000-11-29 2007-09-18 Picoliter Inc. Ejection of localized volumes from fluids
US20020090720A1 (en) * 2000-11-29 2002-07-11 Mutz Mitchell W. Focused acoustic ejection cell sorting system and method
EP2267429A1 (en) 2000-12-28 2010-12-29 Picoliter Inc. Focused acoustic ejection cell sorting system and method
US20110042274A1 (en) * 2008-02-27 2011-02-24 Technische Universiteit Delft Method and Apparatus for the Separation of Solid Particles Having Different Densities
US20110049017A1 (en) * 2008-02-27 2011-03-03 Technische Universiteit Delft Method and Apparatus for Separating Parts, in Particular Seeds, Having Different Densities
US8381913B2 (en) 2008-02-27 2013-02-26 Technische Universiteit Delft Method and apparatus for separating parts, in particular seeds, having different densities
US8418855B2 (en) 2008-02-27 2013-04-16 Technische Universiteit Delft Method and apparatus for the separation of solid particles having different densities
WO2010117273A1 (en) * 2009-04-08 2010-10-14 Technische Universiteit Delft Method and apparatus for separating a non-ferous metal-comprising fraction from ferrous scrap
NL2002730C2 (en) * 2009-04-08 2010-10-11 Univ Delft Tech Method and apparatus for separating a non-ferous metal-comprising fraction from ferrous scrap.
US8678194B2 (en) 2009-04-09 2014-03-25 Technische Universiteit Delft Use of an apparatus for separating magnetic pieces of material
US20130015106A1 (en) * 2010-03-23 2013-01-17 Lins Guenter Device and method for magnetic separation of a fluid
US8844730B2 (en) * 2010-03-23 2014-09-30 Siemens Aktiengesellschaft Device and method for magnetic separation of a fluid
RU2561131C1 (en) * 2014-05-12 2015-08-20 Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Липецкий государственный технический университет" (ЛГТУ) Magnetic divider
US11465157B2 (en) 2020-07-14 2022-10-11 Cláudio Henrique Teixeira Ribeiro Magnetic separators with stationary magnetic matrices, and methods of using the same

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