[0001] The present invention relates to the technical field of a crusher for crushing a
fibrous material and a fiber-containing material such as wheat bran, and the like,
and more particularly, to a mechanical crusher capable of finely crushing a fibrous
material and a fiber-containing material at a high efficiency.
[0002] Mechanical crushers such as the swirl type crusher disclosed in Japanese Examined
Utility Model publication JU. 57-040104 B, the turbo type crusher disclosed in Japanese
Unexamined Patent Application Publication JP. 51-064661 A, and the like have been
used as an apparatus for crushing a powder-like fiber-containing grain material such
as wheat bran to fine powder.
[0003] EP 0 696 475 discloses a pulverizer comprising a frame having an air admitting hole
provided at its lower side part; a material admitting hole and an exit for discharging
pulverized material; a first rotary shaft; a second rotary shaft located inside the
first rotary shaft, wherein both shafts are driven at a lower end; a classifying fan
mounted to the non-driven end of the second rotary shaft; one single disk mounted
on the other end of the first rotary shaft; and a plurality of axe-parallel ribs provided
along an outer circumferential surface of the disk. The frame comprises a liner having
axe-parallel concaves and convexes provided on the inner surface of the frame to face
the ribs on the outer circumferential surface of the disk. Between adjoining ribs
on the disk, a passage is formed and serves as a circulation passage for returning
the material which was pulverized but cannot pass the classifying fan to the gap between
the outer circumferential surface of the disk and the liner.
[0004] DE 197 15 772 discloses a crash swirl mill comprising in inlet portion and an outlet
portion; a lower ventilator disposed in the inlet portion and an upper ventilator
disposed in the outlet portion and having a greater transport capacity than the lower
ventilator. A two-part drum acts as a stator and comprises a bottom, a lower part,
an upper part and a cover and has an inner peripheral wall. A rotor comprises an axis
journaled vertically; a plurality of horizontally extending receiving plates, which
are axially spaced along the axis and comprise openings provided for swirling the
particles in a milling stage; a plurality of vertically extending knives provided
along the peripheral edge of the receiving plate; and separating plates for axially
separating the receiving plates. The plurality of separating plates define therebetween
a plurality of milling stages. The number of the milling stages and the number of
the knives in each receiving plate are selected according to the desired crushing
power of the crash swirl mill and the type of product to be processed.
[0005] EP 775 526 discloses a mechanical grinding apparatus upon which the pre-characterizing
portion of claim 1 is based comprising a rotor constituted by a plurality of rotor
units, supported by a rotary shaft and having a plurality of grooves defined on the
outer peripheral surface thereof; and a liner provided around the outside of the rotor
and having a plurality of grooves defined in the inner peripheral surface thereof
for grinding a substance to be ground in the gap formed between the onter peripheral
surface of the rotor units and the inner peripheral surface of the liner. The grooves
of the rotors all incline in a same direction preventing the flow of the substance
to be ground (particles) with respect to a direction parallel to the rotary shaft.
The keyways of the multiple rotor units are accurately aligned when the rotor units
are secured to the rotary shaft, so that the inclined grooves are smoothly continued
and are not dislocated on the surfaces where the adjacent rotor units join to each
other.
[0006] US 3 640 475 discloses an impact pulverizer comprising a single rotating disc-shaped
supporting element comprising an inner circular row of impact elements and an outer
circular row of impact elements; a housing mantle surrounding the rotating disc, comprising
a stationary filling body and provided with an outer circular row of stationary crushing
elements arranged circumferentially around the rotating crushing grate. The degree
of crushing is controlled by varying the circumferential speed of the crushing elements
and/or the pitch angle of the crushing elements.
[0007] Various types of food that contains fibers are produced and distributed as beauty
foods and health foods. At that time, it is preferable that the particle size of fiber-containing
fine powder is such that a maximum diameter is 100 µm or less and an average diameter
is 30 µm or less in order that these foods taste silky.
[0008] Further, in fiber-like powder for industrial use, for example, carbon fiber and the
like used in a fiber-reinforced composite material, a material having a shorter fiber
length is desired to improve mechanical strength by uniformly blending the fiber-like
powder with a binder.
[0009] In the conventional mechanical crushers as described above, however, the number of
revolutions of a rotor must be increased to obtain fiber-containing fine powder having
the aforementioned particle size with the maximum diameter of 100 µm or less and the
average diameter of 30 µm or less by crushing a fiber-containing material. Thus, various
problems arise in an efficiency of energy, a life of the bearing of the rotor, occurrence
of noise and vibration due to the rotation of the rotor at a high speed, and so on.
[0010] Moreover, since there is a limit in an increase of the number of revolutions of the
rotor, powder and/or grains obtained by crushing a fiber-containing material by the
conventional mechanical crushers are often mixed with powder which is not crushed
to a desired particle size.
[0011] Accordingly, to obtain fiber-containing fine powder having a desired particle size,
it is necessary to execute a process for removing coarse grains the particle size
of which exceeds the desired particle size by means of a classification device such
as a sieve, an air classifier, and the like, from which a problem is arisen in that
a production efficiency is bad.
[0012] Accordingly, an object of the present invention is to solve the problems of the conventional
art and to provide a mechanical crusher for a fiber-containing material capable of
effectively crushing a fiber-containing material used for food such as wheat bran
and a fiber-like material for industrial use such as carbon fiber and the like to
fine powder having a maximum diameter of 100 µm or less and an average diameter of
30 µm or less as a particle size.
[0013] To achieve the above object, as claimed, a mechanical crusher comprises a rotating
shaft extending in an axial direction; a rotor mounted about said rotating shaft and
comprising more than one stage each comprising a sub-rotor each comprising a plurality
of blades; a liner having a plurality of grooves formed on an inner peripheral surface
thereof and disposed externally of said rotor with a predetermined gap defined between
the inner peripheral surface thereof an an outer peripheral surface of said rotor;
and a drive unit for rotating said rotor and coupled to said rotating shaft.
[0014] According to the invention, the rotor comprises varied types of sub-rotors, wherein
(a) the blades of a sub-rotor of one stage incline at a first angle with respect to
the longitudinal direction such that flow of material to be crushed is forced back
upstream of a transportation direction of sufficiently finely crushed material and
blades of a sub-rotor of an adjacent stage incline at a different angle or have no
inclination, and/or
(b) the positions of blades of a sub-rotor of one stage and the positions of blades
of a sub-rotor of an adjacent stage are offset relative to each other in the rotating
direction, and/or
(c) the pitch of said plurality of blades of at least one sub-rotor on said outer
peripheral surface of the rotor in a rotational direction of said rotor is set to
from 8 mm to 40 mm.
[0015] It is preferable that each of the plurality of blades inclines at an angle of 10°
to 45° with respect to the axial direction of the rotating shaft.
[0016] It is also preferable that disc-shaped plate members each having a diameter smaller
than an outermost diameter of the at least one sub-rotor are disposed so as to clamp
each of the sub-rotor in the axial direction of the rotating shaft.
[0017] It is also preferable that the rotor further comprises at least one sub-rotor having
a plurality of blades which are rectangular blades provided in a radial direction
of the rotor and in parallel to the axial direction of the rotating shaft.
[0018] It is further preferable that in alternatives (a) or (b) a pitch of the plurality
of blades on the outer peripheral surface of the rotor in a rotational direction of
the rotor is set to from 8 mm to 40 mm.
[0019] It is still further preferable that a size of the plurality of blades in the rotational
direction is set to from 2 mm to 10 mm and a height of the plurality of blades in
a radial direction of the rotor is set to from half of the pitch of the plurality
of blades to five times the pitch.
[0020] The present invention will be explained in the following non-limiting description
in detail with reference to the attached drawings, in which:
FIG. 1 is a conceptual view showing an embodiment of a crushing apparatus making use
of a mechanical crusher of the present invention;
FIG. 2 is a schematic view partly in cross section showing an embodiment of the mechanical
crusher of the present invention;
FIG. 3 is a front elevational view of an embodiment of a rotor of the mechanical crusher
shown in FIG. 2;
Fig. 4 is a sectional view of the rotor of the mechanical crusher taken along the
line A - A of Fig. 3;
FIG. 5 is a view, partly in enlargement, of the rotor of the mechanical crusher shown
in FIG. 3;
FIGs. 6(A), (B) and (C) are conceptual views showing other embodiments of the rotor
used in the mechanical crusher of the present invention; and .
FIG. 7 is a schematic front elevational view showing another embodiment of the rotor
of the mechanical crusher shown in FIG. 2;
FIG. 8 is a graph showing a 50% particle size when wheat bran is crushed in this example.
FIG. 9 is a graph showing the relationship between the pitch of the blade and the
cumulative 90% minus sieve particle size in the example of the present invention;
and
FIG. 10 is a graph showing the relationship between the pitch of the blade and the
power consumption rate in the example of the present invention.
[0021] The mechanical crusher of the present invention crushes a fiber-containing material
used for food such as wheat bran, and the like and a fiber-like material for industrial
use such as carbon fiber, and the like to fine powder.
[0022] A fiber-containing material handled by the mechanical crusher of the present invention
is not particularly limited, and the mechanical crusher of the invention can crush
various types of fiber-containing materials, for example, a fiber-containing material
used for food that contains a large amount of dietary fiber that is defined as "the
whole difficult-to-digest components contained in food which cannot be broken down
by human digestive enzymen", a fiber-like material for industrial use such as various
types of inorganic and organic materials and so on.
[0023] Preferably exemplified as specific examples which are handled by the mechanical crusher
of the present invention are fiber-containing materials used for food, for example,
wheat bran, been-curd refuse, powdered green tea, dry "wakame", that is, a kind of
seaweed (
Undaria species), dry "hijiki", that is, a kind of brown algae (
Hizikia species), dry laver, dry vegetable, and the like and fiber-like materials for industrial
use, for example, various types of fiber such as carbon fiber, acrylic fiber, aramid
fiber, nylon fiber, silk, and the like, sawdust (wood powder and chips), pulp, and
so on.
[0024] It is preferable that the size of these fiber-containing or fiber-like materials
used for as the crude materials be 20 mm or less and the water content thereof be
10 wt% or less.
[0025] FIG. 1 shows an embodiment of a crushing apparatus for crushing a fiber-containing
material making use of a mechanical crusher (hereinafter, simply referred to as "crusher")
10 of the present invention.
[0026] The illustrated crushing apparatus 50 includes the crusher 10 of the present invention,
a screw feeder 12, a bag filter 14, and a blower 16.
[0027] The fiber-containing material to be crushed as the crude material is supplied to
the material introduction port 18 of the crusher 10 of the present invention by the
screw feeder 12.
[0028] Further, the blower 16 is coupled with the discharge port 20 of the crusher 10 through
the bag filter 14 so that the interior of the crusher 10 (crusher main body 22) is
sucked by the blower 16.
[0029] Accordingly, the fiber-containing material supplied to the introduction port 18 by
the screw feeder 12 is crushed to fine powder while being transported to the upper
portion of the crusher 10 from the introduction port 18 to the discharge port 20 by
the air stream formed by the sucking operation of the blower 16 and discharged from
the discharge port 20.
[0030] The thus discharged fiber-containing fine powder is further transported by the air
stream formed by the blower 16 and taken out after it is captured by the bag filter
14.
[0031] FIG. 2 is a schematic view partially in cross section showing an embodiment of the
crusher 10 of the present invention.
[0032] The crusher 10 of the present invention is composed of the crusher main body 22 and
a rotation device 24.
[0033] The rotation device 24 includes a motor 26, a pulley 29 fixed to the shaft 26a of
the motor 26, a pulley 30 fixed to the lower end of a rotating shaft 38 which will
be described later, and an endless transmission belt 32 trained around the pulleys
28 and 30 with tension. The rotation of the motor 26 rotates the rotating shaft 38,
therefore, a rotor 40 (rotor assembly of the rotor 40 composed of four sub-rotors
41) which will be described later at a predetermined number of revolution. That is
to say, the rotation device 24 functions as a drive unit for rotationg the rotor 40.
[0034] In contrast, the crusher main body 22 is composed of a casing 34 having the introduction
port 18 and the discharge port 20 which were described above, a liner 36 disposed
on the inner surface of the casing 34, the rotating shaft 38, and the rotor 40 mounted
about and fixed to the rotating shaft 38. The rotor 40 may be produced integrally
with the rotating shaft 38, or the rotor 40 and the rotating shaft 38 may be produced
separately and combined with and fixed to each other.
[0035] When necessary, the crusher main body 22 may be cooled by cooling the casing 34 and
the like with water.
[0036] The liner 36 is formed in a cylindrical shape, has a multiplicity of grooves formed
on the inner surface thereof, and is disposed in the inside of the casing 34 so as
to accommodate the rotor 40 with a predetermined gap defined between the inner peripheral
surface (the extreme ends of ribs where the grooves 36a are formed) thereof and the
outer peripheral surface (the extreme ends of blades 44 to be described later) of
the rotor 40. In the invention, the liner 36 may also be a known liner used in various
types of mechanical crusher that uses a rotor and a liner.
[0037] The shape, pitch, and the like of the grooves 36a of the liner 36 are not particularly
limited, and a known liner may be selected and used according to the quality of the
fiber-containing material, the target particle size of fine powder, and the like.
Exemplified as the liner is, for example, a liner including triangular grooves, which
have a depth of 4 mm and are formed at a pitch of 6 mm along the rotating direction
(the peripheral direction of the inner peripheral surface of the liner) of the rotor
40, and extending in the same direction as the rotating shaft 38 (hereinafter, referred
to as an "axial direction").
[0038] Further, the gap defined between the inner peripheral surface of the liner 36 and
the outer peripheral surface of the rotor 40 is not particularly limited. However,
it is preferable to set the gap to about 1 mm to 10 mm because the gap of this size
permits a fiber-containing material to be preferably crushed, and permits fine powder
having a maximum diameter of 100 µm or less and an average diameter of 30 µm or less
to be effectively obtained from a fiber-containing material used for food. It is preferable
that this gap be uniformly formed between the inner peripheral surface of the liner
36 and the outer peripheral surface of the rotor 40.
[0039] The rotating shaft 38 is rotatably journaled between bearings 34a and 34a disposed
on the upper and lower ends of the casing 34. As described above, the pulley 30 of
the rotation device 24 is fixed to the lower end of the rotating shaft 38 that is
rotated by driving the motor 26. Thus, the rotor 40 fixed to the rotating shaft 38
is rotated when the rotating shaft 38 is rotated through the transmission belt 32
by driving the motor 26.
[0040] FIG. 3 shows a schematic front elevational view of the rotor 40 of the crusher 10
of the first aspect of the present invention, and FIG. 4 shows a schematic sectional
view of the rotor 40 taken along the line A-A of FIG. 3, respectively.
[0041] The rotor 40 of the crusher 10 is mainly related to the crushing of a fiber-containing
material to be crushed.
[0042] As shown in FIGs. 3 and 4, the rotor 40 is formed in a cylindrical shape with the
center thereof in coincidence with the center of rotation of the rotating shaft 38
and includes a central section 42 fixed to the rotating shaft 38 and the blades 44
that are formed in a rectangular plate shape and project from the outer peripheral
surface of the central section 42 in radial directions. These blades 44 are provided
in a predetermined number (16 pieces in the exemplified example) at predetermined
intervals in a rotational direction (peripheral direction of the central section 42).
Note that, in FIG. 3, the extreme end surfaces of the blades 44 are shown with recticulations
to make the arrangement thereof distinct.
[0043] The rotor 40 also may be arranged by integrally producing the blades 44 and the central
section 42, or the rotor 40 may be arranged by separately producing the blades 44
and the central section 42 and combining and fixing them with and to each other.
[0044] Note that, in the crusher 10 of the present invention, the sectional shape of the
blades 44 is not limited to the rectangular plate shape of the illustrated embodiment
shown in FIG. 4, and various types of shape such as a triangular shape, and the like
used in known mechanical crushers can be utilized. However, in the present invention,
since the fiber-containing material is basically crushed by being impacted and struck
with the blades 44 of the rotor 40, it is preferable to form the cross section of
the blades 44 in the rectangular plate shape as shown in the illustrated embodiment.
[0045] As a preferable aspect of the illustrated crusher 10, a single rotor (the rotor assembly)
40 is arranged by stacking sub-rotors 41a, 41b, 41c and 41d in four stages in the
axial direction and disposing disc-shaped partitions 46 so as to clamp the sub-rotors
41a to 41d, which constitute the entire rotor 40, in the axial direction.
[0046] Note that the partitions 46 may be produced integrally with the sub-rotors 41a to
41d of the rotor 40, or the partitions 46 and the sub-rotor 40a to 40d of the rotor
40 may be separately produced and combined and fixed with and to each other.
[0047] The rotor may be arranged by stacking a plurality of sub-rotors and disposing each
of the disk-shaped partitions between the adjacent sub-rotors and outside of both
outermost sub-rotors in the axial direction.
[0048] In the illustrated embodiment, the uppermost stage sub-rotor 41a has the characteristic
arrangement of the present invention. That is, the blades 44 of the uppermost stage
sub-rotor 41a incline in a direction where the flow of a material to be crushed is
forced back, while the blades 44 of the other sub-rotors 41b to 41c are disposed so
as to extend in the axial direction.
[0049] In the crusher 10 of the present invention, at least one of the sub-rotors 41a to
41d has the inclining blades 44, which permits the fiber-containing material such
as wheat bran and the fiber-like material such as carbon fiber, and the like to be
effectively crushed to fine powder.
[0050] FIG. 5 schematically shows the action of the blades 44 that incline in the direction
where the material to be crushed is forced back.
[0051] Note that, in the present invention, the expression that "the blades of the rotor
(sub-rotor) incline in the direction where the material to be crushed is forced back"
means that the blades 44 of the rotor 40 (sub-rotor 41) in rotation (in the direction
of an arrow x) generate an air stream in a direction opposite to the direction where
the material to be crushed (fiber-containing material) w which is supplied into the
crusher 10 is transported therein (the direction of an arrow y in the figure).
[0052] As shown in FIG. 5, the material to be crushed w is transported in the direction
of the arrow y by the air stream generated by the blower 16, collides against the
blades 44 of the rotor 40 in rotation, and is crushed thereby.
[0053] Grains having a large size are liable to fall into the space (pocket) between the
adjacent blades 44 and to collide against the blades 44 because they are unlikely
to be flown by the air stream. In addition to the above-mentioned, after these grains
collide against the blades 44, they are forced back upstream (direction opposite to
the direction where they are transported by the air stream) by the action of the inclining
blades 44 as shown by an arrow z. That is, fine grains that have been crushed sufficiently
are transported downstream by the air stream generated by the blower 16 and discharged
from the crusher 10. In contrast, grains having a large size are forced back by the
inclining blades 44, repeat collision against the blades 44, and are subjected to
a crushing operation many times until they are sufficiently crushed.
[0054] The crusher 10 of the present invention permits the fiber-containing material and
the fiber-like material, which cannot be finely crushed by the conventional crusher
apparatus effectively, to be crushed to fine powder effectively.
[0055] In the crusher 10 of the present invention, the inclining angle of the blades 44
(angle θ shown in FIG. 5) is not particularly limited and the blades 44 may incline
at any angle in the above direction in which the material to be crushed is forced
back, that is, the inclining angle θ may be set to any angle exceeding 0° and less
than 90°. In particular, it is preferable to set the inclining angle to 10° to 45°
because fine crushing can be effectively executed at any angle set within the range
of these angles.
[0056] As described above, in the illustrated crusher 10, the single rotor is constructed
by stacking the sub-rotors 41a to 41d of the four stages in the axial direction through
the disc-shaped partitions 46, and the blades 44 of only the uppermost stage sub-rotor
41a incline.
[0057] In the sub-rotor 41b of a second stage (hereinafter, the number of stages is counted
from the upper side) to the lowermost stage sub-rotor 41d, adjacent sub-rotors are
disposed such that the positions of the blades 44 thereof are offset in a rotating
direction (direction of an arrow x in FIGS. 3 and 4) relative to each other. That
is, in FIG. 3, a third stage sub-rotor shows a state in which the rotor 40 is viewed
in the direction of an arrow a in FIG. 4, and a second stage sub-rotor and a lowermost
stage sub-rotor show a state in which the rotor 40 is viewed from the direction of
an arrow b in FIG. 4.
[0058] As described above the rotor 40 is composed of at least two stages of the sub-rotors
and further the positions of the blades 44 are offset in the rotating direction in
stages of the rotors adjacent to each other in the axial direction, whereby the fiber-containing
material and the fiber-like material can be crushed more preferably.
[0059] Note that when the crusher 10 is constructed by the rotor 40 including a plurality
of stages, the number of the stages is not particularly limited.
[0060] Further, when the rotor 40 has a plurality of stages of sub-rotors as shown in the
illustrated embodiment, the respective sub-rotors 41a to 41d (and the partitions 46)
may be produced integrally, or the sub-rotors and the partitions may be produced separately
and combined with and fixed to each other.
[0061] As described later, however, it is possible in the crusher of the present invention
to combine various types of sub-rotors. Accordingly, it is preferable to combine sub-rotors
produced separately and to combine and fix them with and to each other to cope with
a variation of the combinations thereof.
[0062] As a preferable aspect of the illustrated crusher 10, the partitions 46 are disposed
so as to clamp the respective sub-rotors 41a to 41d in the axial direction. While
the partitions 46 are not essential in the present invention, the provision of them
can more improve the crushing efficiency of the fiber-containing material and the
fiber-like material.
[0063] Note that the size of the partitions 46 is not particularly limited. According to
the examination of the inventors, however, it is preferable that the size of the partitions
46 be slightly smaller than the outermost diameter (the extreme end of the blades
44) of the rotor 40. In particular, it is preferable that the size of the partitions
46 be smaller than the outermost diameter of the rotor 40 by 2 mm to 40 mm in radius.
[0064] The illustrated crusher 10 has the rotor 40 composed of the sub-rotors 41a to 41d
of the four stages, and the blades 44 of only the uppermost stage sub-rotor 41a incline
in the direction where the flow of the material to be crushed is forced back (hereinafter,
simply referred to as "incline"). However, the combination of the sub-rotors in the
crusher of the present invention is not limited thereto and various combinations are
possible as described in the following.
[0065] For example, as schematically shown in FIG. 6A, sub-rotors 41a and 41b having blades
44 that incline similarly may be used in uppermost and second stages, respectively,
a sub-rotor 41c having blades 44 that incline at a small angle may be used in a third
stage, and a sub-rotor 41d having blades 44 without inclination may be used in a lowermost
stage.
[0066] Otherwise, as shown in FIG. 6B, a sub-rotor 41a having blades 44 that incline at
a large angle may be used in an uppermost stage, a sub-rotor 41c having blades 44
that incline at a small angle may be used in a third stage, and sub-rotors 41b and
41d having blades 44 without inclination may be used in second and lowermost stages
respectively.
[0067] Further, as shown in FIG. 6C, sub-rotors 41b and 41d having blades 44 that incline
in a direction opposite to the direction where the flow of the material to be crushed
is forced back may be combined with sub-rotors 41a and 41c having blades 44 that incline
in the direction where the flow of the material to be crushed is forced back.
[0068] In the present invention, sub-rotors 41a to 41d having blades 44 that incline similarly
may be used in all the stages, sub-rotors 41a to 41d having blades 44 that incline
at a different angle may be used in all the stages, and a sub-rotor 41d having inclining
blades 44 may be used only in the lowermost stage, in addition to the above arrangements.
That is, the present invention can use various combinations of sub-rotors 41.
[0069] Further, while all of the above examples have the four-stage sub-rotors, the present
invention is by no means limited thereto as described above.
[0070] In the sub-rotors 41 of the crusher 10 of the present invention, the pitch P of the
blades 44 on the outer peripheral surface thereof, the thickness c of the blades 44,
and the height h of the blades 44 (length of the central section 42 in a radial direction)
are not particularly limited and may be suitably determined according to the scale
and the like of the crusher 10, regardless of whether the blades 44 of the sub-rotors
incline or not.
[0071] According to the examination of the inventors, as described above, it is preferable
that the pitch P of the blades 44 be set to 8 mm to 40 mm, that the thickness c of
the blades 44 be set to 2 mm to 10 mm, and that the height h of the blades 44 be set
to half of the pitch F of the blades 44 to five times the pitch P, more preferably
one to five times the pitch P of the blades 44, respectively.
[0072] Satisfying at least one or all of the above conditions permits the fiber-containing
material and the fiber-like material to be crushed more preferably and more excellent
fine powder of fiber to be obtained.
[0073] A method of producing the sub-rotors 41 and the rotor 40 is not particularly limited
and any known method such as cutting and the like can be used. Further, after the
rotor 40 is produced, the hardness of the surface thereof may be improved by a method
such as induction hardening, thermal spraying, CVD coating, or the like.
[0074] Further, a material for forming the rotor 40 is not particularly limited, and a steel
material such as SS, S45C, etc., for example, may be used.
[0075] In the crusher 10 of the present invention having the rotor 40 arranged as described
above, the rotational speed of the rotor 40 is not particularly limited.
[0076] However, it is preferable to set such a rotational speed that the peripheral speed
of the rotor 40 is set to 60 m/sec to 160 m/sec, in particular 80 m/sec to 140 m/sec
on the outer peripheral surface thereof in order to execute crushing excellently.
[0077] Furthermore, in the rotor 40 of the crusher 10 of the present invention, as shown
in FIG. 7, a plurality of blades 44 of the sub-rotors 41 in all the stages may be
blades in the rectangular plate shape which have no inclination, that is to say, which
extend from the center section 42 of the rotor 40 in radial directions and are positioned
longitudinally in parallel with the axial direction of the rotating shaft 38. It should
be noted that Fig. 4 may be also accounted a sectional view of the second stage sub-rotor
41 of the rotor 40 shown in Fig. 7.
[0078] Also in the rotor 40 shown in FIG. 7, adjacent sub-rotors 41 are disposed such that
the positions of the blades 44 thereof are offset in a rotating direction (direction
of an arrow x in FIGs. 7 and 4) relative to each other, as is the case with the rotor
40 shown in FIG. 3. That is, in FIG. 7, an uppermost stage and a third stage show
a state in which the sub-rotors 41 are viewed in the direction of an arrow a in FIG.
4, and a second stage and a lowermost stage in FIG. 7 show a state in which the sub-rotors
41 are viewed from the direction of an arrow b in FIG. 4. In this case also, the rotor
40 is composed of at least two stages of the sub-rotors 41 and the positions of the
blades 44 are offset in the rotating direction in stages adjacent to each other in
the axial direction, whereby the fiber material such as the fiber-containing material
and the fiber-like material can be crushed more preferably.
[0079] When the rotor 40 shown in FIG. 7 is used, it is required that the blades 44 of each
of sub-rotors 41 as stated above be arranged such that the pitch P shown in FIG. 4,
which is the pitch of the blades 44 in the rotating direction on the outer peripheral
surface of the sub-rotor 41 (pitch of the extreme ends of the blades 44), is 8 mm
to 40 mm, preferably 10 mm to 30 mm.
[0080] As mentioned before, when a fiber material such as a fiber-containing material and
a fiber-like material is to be crushed to fine powder having a particle size of 100
µm or less by any conventional mechanical crusher, it is necessary, for example, to
increase the number of revolutions of the rotor 40 and a problem of low efficiency
occurs because crushing can not be effected desirably with such crushers.
[0081] In contrast, according to the present invention, it is possible to crush a fiber
material such as wheat bran to fine powder having a particle size of 100 µm or less
by setting the pitch P of the blades 44 on the outer peripheral surface of the rotor
(hereinafter referred to as "blade pitch P") to 8 mm to 40 mm. The fine powder thus
obtained can be suitably added to various foods.
[0082] As will be evident from the Example 7 stated below, if the blade pitch P is larger
than 40 mm, the efficiency in crushing of a fiber material is decreased and fine powder
of fiber crushed to a particle size of 100 µm or less can not be obtained at a high
efficiency.
[0083] On the other hand, the crushing efficiency is again decreased with the blade pitch
P which is too small. If the blade pitch P is smaller than 8 mm, fine powder of fiber
crushed to a particle size of 100 µm or less can also not be obtained at a high efficiency.
[0084] Also in the rotor 40 shown in FIG. 7, the thickness c (the size in the rotating direction)
of the blades 44 is not particularly limited and is preferably 2 mm to 10 mm.
[0085] The height h (the length in a radial direction of the center section 42) of the blades
44 of this rotor 40 is also not particularly limited. It is preferably half of the
blade pitch P to five times the blade pitch P, more preferably one to five times the
blade pitch P.
[0086] Satisfying one, or both espetially, of above two conditions permits the fiber-containing
material and the fiber-like material to be crushed more preferably and more excellent
fine powder of fiber to be obtained.
[0087] In the examples as described above, the rotating shaft 38 is arranged vertically,
although the present invention is not limited to such an arrangement. The rotating
shaft 38 may also be arranged horizontally, for example.
[0088] While the mechanical crusher of the present invention has been described above in
detail, the present invention is by no means limited to the aforementioned embodiments
and it goes without saying that various improvements and modifications can be made
within the range which does not depart from the scope of the present invention as
defined by the appended claims.
[Examples]
[0089] The present invention will be described in more detail by exemplifying specific examples
of crushing carried out by the mechanical crushers of the present invention. It is
needless to say that the present invention is not limited thereto.
[Example 1]
[0090] A crusher 10 of the first aspect of the present invention was produced which was
arranged such that a rotor 40 shown in Fig 3. had a diameter (extreme end of blades
44) of 150 mm, the gap between the rotor 40 and a liner 36 was set to 2 mm, the height
h of the blades 44 was set to 20 mm, the thickness c of the blades 44 was set to 6
mm, the number of the blades 44 was set to 16 pieces, the height of a single sub-rotor
41 was set to 45 mm, the number of stages of the sub-rotors 41 of the rotor 40 was
set to four states, the diameter of partitions 46 was set to 136 mm, and the thickness
of the partitions 46 was set to 5 mm. The crusher apparatus 50 shown in FIG. 1 was
constructed using the crusher 10 and wheat bran having a particle size of about 2
mm was crushed thereby.
[0091] Wheat bran was supplied through a screw feeder 12 in an amount of 1 kg/hr. Further,
the number of revolution of the rotor 40 was set to 10,000 rpm to 14,000 rpm, and
the volume of air supplied from a blower 16 was set to 2 m
3/min.
[0092] Under the above conditions, wheat bran was crushed by replacing the uppermost stage
sub-rotor 41a of the crusher 10 with three types of sub-rotors 41 the inclining angle
θ of the blades 44 of which was set to 0°, 15°, and 30°, respectively. Note that the
inclining angle of the blades 44 of the sub-rotors 41b, 41c and 41d of the stages
other than the uppermost stage was set to 0°.
[0093] The 50% particle size of the wheat bran having been crushed was measured with a dry
type laser particle size measuring instrument (Microtrack), and FIG. 8 is a graph
showing the result of measurement.
[0094] In FIG. 8, a symbol ○ indicates the result of measurement when the sub-rotor 41a
the blades 44 of which had the inclining angle θ set to 0° was used, a symbol ▲ indicates
the result of measurement when the sub-rotor 41a the blades 44 of which had the inclining
angle θ set to 15° was used, and a symbol × indicates the result of measurement when
the sub-rotor 41a the blades 44 of which had the inclining angle θ set to 30° was
used, respectively. As apparent from the graph, the crusher of the present invention
could crash wheat bran more finely as compared with the case in which wheat bran was
crushed with the crusher of the second aspect of the present invention as the reference
example when the wheat bran was crushed under the same conditions, and further the
number of revolution of the rotor of the crusher of the first aspect of the present
invention could be greatly reduced when the same particle size was obtained in crushing,
whereby the crushing capability of the crusher of the first aspect of the present
invention could be greatly improved.
[Example 2]
[0095] A crusher 10 was constructed similarly to the Example 1 except that the inclining
angle θ of the blades 44 of uppermost stage and second stage sub-rotors 41a and 41b
was set to 30° and that the inclining angle θ of the blades 44 of a third stage sub-rotor
40c was set to 15° as shown in FIG. 6A. Wheat bran was crushed using the crusher 10
similarly to the Example 1 except that the number of revolution of a rotor 40 was
fixed to 14,000 rpm.
[0096] When the 50% particle size of the wheat bran having been crushed was measured similarly
to the Example 1, it was 9.5 µm, whereby it was confirmed that the wheat bran could
be crushed more finely as compared with the case in which wheat bran was crushed with
the crusher of the Example 1 and the reference example.
[Example 3]
[0097] A crusher 10 was constructed similarly to the Example 1 except that the pitch P of
the blades 44 of second stage to lowermost stage sub-rotors 41b to 41d was set to
one half of that of the blades 44 of the Example 1 and that the number of the blades
44 was set to 32 pieces. Wheat bran was crushed using the crusher 10 similarly to
Example 1 except that the number of revolutions of a rotor 40 was fixed to 10,000
rpm.
[0098] When the 50% particle size of the wheat bran having been crushed was measured similarly
to the Example 1, it was 26 µm whereby it was confirmed that the wheat bran could
be crushed more finely as compared with the case in which wheat bran was crushed with
the crusher as the reference example.
[Example 4]
[0099] A crusher 10 was constructed similarly to the Example 1 except that the inclining
angle θ of the blades 44 of an uppermost stage sub-rotor 41a was set to 30° and the
inclining angle θ of the blades 44 of a third stage sub-rotor 41c was set to 15°,
as shown in FIG. 6B. Wheat bran was crushed using the crusher 10 similarly to the
Example 1 except that the number of revolution of a rotor 40 was fixed to 14,000 rpm.
[0100] When the 50% particle size of the wheat bran having been crushed was measured similarly
to the Example 1, it was 17.6 µm, whereby it was confirmed that the wheat bran could
be crushed more finely as compared with the case in which wheat bran was crushed with
the crusher as the reference example.
[Example 5]
[0101] A crusher 10 was constructed similarly to the Example 1 except that the inclining
angle θ of the blades 44 of an uppermost stage sub-rotor 41a was set to 30°, the inclining
angle θ of the blades 44 of a second stage sub-rotor 41b was set to -30°, the inclining
angle θ of the blades 44 of a third stage sub-rotor 41c was set to 30°, and the inclining
angle θ of the blades 44 of a lowermost stage sub-rotor 41d was set to -30° as shown
in FIG. 6C. Wheat bran was crushed using the crusher 10 similarly to the Example 1
except that the number of revolution of a rotor 40 was fixed to 14,000 rpm.
[0102] When the 50% particle size of the wheat bran having been crushed was measured similarly
to the Example 1, it was 21.6 µm, whereby it was confirmed that the wheat bran could
be crushed more finely as compared with the case in which wheat bran was crushed with
the crusher as the reference example.
[Example 6]
[0103] Polyamide resin having a fiber length of about 0.2 mm was crushed with a crusher
apparatus 50 similarly to the Example 3 (that is, using the same crusher 10 as the
Example 3). The polyamide was supplied through a screw feeder 12 in an amount of 0.3
kg/hr, the number of revolution of a rotor 40 was set to 14,000 rpm, and the amount
of air supplied from a blower 16 was set to 2 m
3/min.
[0104] When the 50% particle size of a resulting crushed product was measured with a wet
type laser particle size measuring instrument (Microtrack), it was 24 µm. When polyamide
resin was crushed using the crusher of the reference example in Example 1 under the
same conditions, the 50% particle size of a resulting crushed product was 48 µm, whereby
it was confirmed that the polyamide resin could be crushed more finely as compared
with the case in which polyamide resin was crushed with the crusher of the reference
example.
[Example 7]
[0105] In the crusher apparatus 50 shown in FIG. 1, wheat bran was crushed with varying
blade pitch P of respective sub-rotors 41 of the rotor 40 in the crusher main body
22 as shown in FIG. 7.
[0106] In the rotor 40 (sub-rotors 41) used, the rotor diameter (the maximum diameter as
measured to the extreme ends of blades 44) was 150 mm, and the height h of the blades
44 was 40 mm, their thickness c was 6 mm and their size in the axial direction was
50 mm. In the case of the rotor with the blade pitch P of about 6 mm, the thickness
c of the blades 44 was changed into 4 mm and their height h into 8 mm for reasons
of production and arrangement. In the crusher main body 22, four stages of sub-rotors
41 were stacked to a single rotor 40, as shown in FIG. 7.
[0107] As the liner 36 was used a liner including triangular grooves 36a of a 4 mm depth
extending in the axial direction, which were formed in the inner peripheral surface
of the liner 36 at a pitch of 6 mm along the rotating direction.
[0108] Using the crusher apparatus 50 comprising such components as above, wheat bran having
a particle size of about 2 mm, which was supplied through the screw feeder 12 at a
rate of 5 kg/hr, was crushed under suction by the blower 16 at an air flow rate of
1.5 m
3/min.
[0109] FIG. 9 shows the relationship between the blade pitch P and the cumulative 90 % minus
sieve particle size (the particle size in which the cumulative size distribution (the
under size distribution) is 90%) when the number of revolution of the rotor 40 was
set to 14,000 rpm (corresponding to an air velocity of 109.9 m/sec).
[0110] As seen from FIG. 9, according to the present crusher 10, wherein the blade pitch
P is 8 mm to 40 mm, it is possible to crush wheat bran suitably to obtain fine powder
having a particle size of 100 µm or less at a high efficiency.
[0111] Further, FIG. 10 shows the relationship between the blade pitch P and the power required
for crushing a material of a unit weight (power consumption rate) when the number
of revolutions of the rotor 40 was adjusted such that the crushed product had the
cumulative 50 % minus sieve particle size of 20 µm.
[0112] As seen from FIG. 10, according to the present crusher 10, wherein the blade pitch
P is 8 mm to 40 mm, it is possible to finely crush wheat bran with an energy efficiency
higher than ever.
[0113] The advantage of the present invention will be apparent from the above results.
[0114] As described above in detail, according to the mechanical crusher of the present
invention, fiber materials including a fiber-containing material used for food such
as wheat bran and the like and a fiber-like material for industrial use such as carbon
fiber and the like can be more finely crushed at a high efficiency, making it possible
to obtain fine powder of fiber having a particle size of 100 µm or less at a high
efficiency, for example.
[0115] Consequently, if the present invention is applied to foods, for example, those health
foods and beauty foods can be desirably produced which contain fine powder of fiber
and yet have pleasant feels in the mouth, as tasting silky or being smooth on the
tongue, for example.