Incorporation by Reference
Technical Field
[0002] The present invention relates to a stirring impeller intended for mixing and a stirring
device including the same.
Background Art
[0003] In the related art, for example, a stirring device including a cylindrical stirred
tank, a stirring shaft disposed at a central part of the stirred tank, and a stirring
impeller attached to a lower part side of the stirring shaft is known as a stirring
device that stirs an object to be stirred.
[0004] Additionally, a stirring impeller including a plate-shaped member attached to the
stirring shaft and a plurality of flat plate-shaped blade parts fixed to an outer
peripheral side of the plate-shaped member is known as a stirring impeller provided
in this type of stirring device. According to this stirring device, if the stirring
shaft rotates around an axis center, the stirring impeller rotates together with the
stirring shaft, and the object to be stirred is stirred and mixed by this rotation.
[0005] However, in a case where the object to be stirred is stirred using such a stirring
impeller, a lot of cavities maybe generated on back sides of the flat plate-shaped
blade parts (cavitation) . In that case, there is a concern that stirring efficiency
may degrade.
[0006] Thus, a stirring impeller configured so that a longitudinal section of each blade
part has a shape that is curved or bent in a direction opposite to the rotational
direction of the blade part is suggested (refer to Japanese Unexamined Patent Application
Publication No.
2004-35724). According to this stirring impeller, cavitation is suppressed.
Citation List
Patent Literature
[0007] [PTL 1] Japanese Unexamined Patent Application Publication No.
2004-35724
Summary of Invention
Technical Problem
[0008] However, also in the stirring impeller as illustrated in the Japanese Unexamined
Patent Application Publication No.
2004-35724, cavitation occurs on the back side of the blade part. For this reason, it cannot
still be said that suppression of cavitation is sufficient. Additionally, since the
resistance that the stirring impeller receives from the object to be stirred is relatively
strong, a large driving force is required in an amount equal to the resistance. In
this way, it cannot be said that the above stirring impeller has sufficient stirring
efficiency, and a stirring impeller with further improved stirring efficiency is desired.
[0009] An object of the invention is to provide a stirring impeller with improved stirring
efficiency and a stirring device including the same, in view of the above problems.
Solution to Problem
[0010] A stirring impeller related to the invention is a stirring impeller to be attached
to a stirring shaft provided in a stirring device. The stirring impeller includes
a plate-shaped support part that is attached to the stirring shaft; and a plurality
of blade units that are disposed on an outer peripheral edge side of the support part.
The support part includes a first surface and a second surface. Each of the blade
units includes a first blade part that protrudes from one of the first surface and
the second surface in the support part, a second blade part that protrudes from the
other one of the first surface and the second surface in the support part and is made
unsymmetrical to the first blade part, and an opening that is formed in at least one
of the first blade part and the second blade part.
[0011] Additionally, in the stirring impeller of the above configuration, the support part
may be formed in a circular shape. The plurality of blade units may be provided at
predetermined intervals along a circumferential direction of the support part. The
first blade part in one of two blade units adjacent to each other in the circumferential
direction of the support part may be provided on the first surface of the support
part, the first blade part in the other one of the two adjacent blade units may be
provided on the second surface of the support part, the second blade part of the one
blade unit may be provided on the second surface of the support part, and the second
blade part of the other blade unit may be provided on the first surface of the support
part.
[0012] Additionally, regarding the first blade part and the second blade part that are made
asymmetrical to each other, for example, a configuration in which the first blade
part is formed in a linear shape and the second blade part is formed in a curved shape
may be adopted.
Brief Description of Drawings
[0013]
Fig. 1 is a schematic longitudinal sectional view of a stirring device including a
stirring impeller related to a first embodiment of the invention.
Fig. 2 (a) is a top view of the stirring impeller related to the present embodiment.
Fig. 2 (b) is a sectional view as seen in the direction of arrow X-X of Fig. 2(a).
Fig. 3 is a partial side view illustrating an example of a blade unit in the stirring
impeller related to the present embodiment.
Fig. 4(a) is a top view of the stirring impeller related to the present embodiment
provided for a performance test. Fig. 4(b) is a sectional view as seen in the direction
of arrow X-X of Fig. 4(a).
Fig. 5 illustrates test data of the performance test. An upper graph is a graph illustrating
the relationship between ventilation volume and kLa (overall mass transfer capacity
coefficient). A lower graph is a graph illustrating the relationship between the ventilation
volume and power (per unit volume) transmitted to liquid.
Description of Embodiments
[0014] Hereinafter, a stirring impeller related to a first embodiment of the invention together
with a stirring device including this stirring impeller will be described referring
to Figs. 1 to 3. In addition, in Fig. 1, the stirring impeller 4 is schematically
illustrated by a dashed line, and the stirring impeller 4 is illustrated in detail
in Figs. 2 and 3.
[0015] A stirring device 1 including the stirring impeller 4 of the present embodiment is
a vertical stirring device. The stirring device 1 includes a stirred tank 2 that contains
an object (liquid L) to be stirred, a stirring shaft 3 that is rotatably attached
within the stirred tank 2, the stirring impeller 4 that is attached to the stirring
shaft 3, and a driving unit 5 that rotates the stirring shaft 3. Additionally, the
stirring device 1 further includes a gas supply unit 6 that supplies another object
(gas G) to be stirred into the stirred tank 2 from a bottom part 22 of the stirred
tank 2. In addition, in the present embodiment, objects to be stirred that are contained
in the stirred tank 2 are the liquid L and the gas G. Although a case where the gas
G is dispersed in liquid is described below as an example, the kind of object to be
stirred is not particularly limited. Additionally, the liquid L also includes liquid
or the like with higher viscosity and lower flowability other than liquid with lower
viscosity and higher flowability.
[0016] The stirred tank 2 is formed in a cylindrical shape that is long in a longitudinal
direction. Specifically, the stirred tank 2 includes a cylindrical body part 21, a
bottom part 22 that is attached to a lower end of the body part 21 and is semi-elliptical,
dish-shaped, or the like in sectional shape, and a top part 23 that is attached to
an upper end of the body part 21 and is semi-elliptical, dish-shaped, or the like
in sectional shape. Additionally, the stirred tank 2 holds the stirring shaft 3 so
that an axial center direction A of the stirring shaft 3 coincides with a vertical
direction (upward-downward direction of Fig. 1).
[0017] The stirring shaft 3 is disposed at a central part of the stirred tank 2. A lower
end part of the stirring shaft 3 is supported via a bearing (not illustrated) provided
at the bottom part 22 of the stirred tank 2. Meanwhile, an upper end part of the stirring
shaft 3 extends above the top part 23 of the stirred tank 2, and is connected to the
driving unit 5 (here, for example referred to as a motor M.) disposed above the top
part 23. The stirring shaft 3 rotates under the driving of the driving unit 5. In
addition, a configuration in which the lower end part of the stirring shaft 3 is not
supported at all may be adopted as the stirring shaft 3. Additionally, a configuration
in which the lower end part of the stirring shaft 3 extends below the bottom part
22 and is connected to the driving unit 5 disposed below the bottom part 22 may be
adopted.
[0018] As illustrated in Figs. 2 and 3, the stirring impeller 4 includes a cylindrical boss
41 that is attached to the stirring shaft 3, a tabular or circular (disk-shaped or
doughnut-shaped) support part 42 that extends in a radial direction B of the stirring
shaft 3 from the boss 41, and a plurality of blade units 43 that are attached to a
peripheral edge part (outer peripheral edge side) of the support part 42. The support
part 42, the boss 41, and the blade units 43 are fixed by welding or the like, respectively.
[0019] As illustrated in Fig. 2 (a), the boss 41 has a through-hole 41a inserted through
the stirring shaft 3. As for the stirring impeller 4, the stirring shaft 3 is inserted
through the through-hole 41a of the boss 41. The stirring impeller 4 is attached to
the stirring shaft 3 by the boss 41 and the stirring shaft 3 being screw-fastened,
welded, or the like.
[0020] The support part 42 is formed to protrude to the outer peripheral side in the radial
direction B from an outer peripheral surface of the boss 41 so that the boss 41 is
located at the center thereof. Additionally, the support part 42 is fixed to the boss
41 so as to be orthogonal to the axial center direction A of the stirring shaft 3.
The length of the support part 42 in the radial direction B of the boss 41 can be
appropriately designed according to the radius of the stirred tank 2, or the like,
and can be, for example, about 20 to 50% of the diameter of the stirred tank 2, although
not particularly limited.
[0021] As illustrated in Fig. 2(a), the plurality of blade units 43 (six in the illustrated
example) are arranged at predetermined intervals along a circumferential direction
of the support part 42. Each blade unit 43 is arranged so as not to jump out outward
in the radial direction from the outer peripheral edge of the support part 42. In
the present embodiment, an outer peripheral edge of each blade unit 43 and the outer
peripheral edge of the support part 42 coincide with each other in a plan view. As
illustrated in Fig. 2(b), the blade unit 43 has a first blade part 43a that protrudes
from an upper surface (first surface) 42a that is one surface of the support part
42 and is formed in a linear shape viewed in the radial direction, and a second blade
part 43b that protrudes from a lower surface (second surface) 42b that is the other
surface of the support part 42 and is formed in a curved shape viewed in the radial
direction. Additionally, one end of the blade unit 43 is fixed to the support part
42, and the other end of the blade unit 43 is arranged at a certain distance from
the support part 42. The support part 42 is rotated toward a side where the blade
unit 43 is released.
[0022] Since the first blade part 43a is formed in a linear shape viewed in the radial direction
and the second blade part 43b is formed in a curved shape viewed in the radial direction,
both of the blade parts 43a and 43b have asymmetrical shapes on the basis of the support
part 42. The first blade part 43a is fixed to one surface of the support part 42 in
a thickness direction. The second blade part 43b is fixed to the other surface of
the support part 42.
[0023] The first blade part 43a has an opening 44 at apart thereof. The opening 44, as illustrated
in Fig. 2, is formed such that predetermined regions on a root side and a radial outer
side of the first blade part 43a are cut off in a linear shape, and has a space through
which an object to be stirred passes. In addition, the opening 44 may be formed in
the second blade part 43b. That is, the opening 44 may be formed in at least one (one
or both) of the first blade part 43a and the second blade part 43b. The second blade
part 43b is formed in a circular-arc curved shape viewed in the radial direction.
This curved shape is not limited to a circular-arc shape, and may be, for example,
a shape in which a plurality of linear portions are connected.
[0024] The circular-arc curved shape of the second blade part 43b is, specifically, a shape
that is indicated in Fig. 2(a) and that is cured with a constant curvature radius
(for example, a curvature radius m5 illustrated in Fig. 4(b)) between two end edges
having a parallel relationship with a one-dot chain line showing a receding angle
α. In addition, although the second blade part 43b of the present embodiment is curved
with the constant curvature radius m5, the invention is not limited to this, and the
second curved part may be formed, for example, in a shape that is curved with different
curvature radii depending on portions. Specifically, the second blade part has a shape
of which the curvature radius is made different partially from the side of the second
blade part 43b fixed to the support part 42 toward an end part of the second blade
part 43b.
[0025] Additionally, although the second blade part 43b of the present embodiment is formed
with the same curvature radius in a direction along a one-dot chain line showing the
receding angle α, the invention is not limited to this, and the second blade part
may have different curvature radii in this direction. Specifically, the curvature
radius of the second blade part 43b may also be changed from the outer peripheral
side of the support part 42 toward the center side of the support part 42.
[0026] Additionally, the center side of the curvature radius in the second blade part 43b,
as illustrated in Fig. 4, is located on the first blade part 43a, that is, on the
support part 42 side. That is, the second blade part 43b has a shape that becomes
concave with respect to the support part 42. Since the second blade part 43b is formed
so that the center side of the curvature radius becomes the support part 42 side and
the curved surface of the second blade part 43b protrudes in a direction away from
the support part 42, the separation vortex of an object to be stirred that passes
through an outer peripheral part of the first blade part 43a is not easily generated
when the supporting part 42 has rotated in the direction (in the direction of the
end part of the second blade part 43b) of an illustrated arrow.
[0027] As for a blade unit 43 and another blade unit 43 adjacent thereto in the circumferential
direction in Fig. 2(b), the position of the first blade part 43a and the position
of the second blade part 43b are reversed. More specifically, as for one blade unit
43 (the blade unit 43 illustrated in Fig. 2(b)) of two adjacent blade units 43, the
first blade part 43a is formed on the first surface 42a of the support part 42. However,
in the case of the other blade unit 43, the second blade part 43b is formed on the
first surface 42a of the support part 42. Similarly, the second blade part 43b of
one blade unit 43 is formed on the second surface 42b of the support part 42. However,
in the case of the other blade unit 43, the first blade part 43a is formed on the
second surface 42b of the support part 42.
[0028] Additionally, the arrangement and the size of the opening 44 between the first blade
part 43a or the second blade part 43b are not particularly limited, and may be appropriately
set so that suppression of cavitation and suppression of the strength reduction of
the blade unit 43 are achieved. For example, the opening 44 may be formed on a tip
side in the first blade part 43a or the second blade part 43b, or may be formed on
a radial inner side. Moreover, although the opening 44 is formed so as to be cut off
in a linear shape in the present embodiment, the opening may be formed so as to be
cut off in a curved shape. Additionally, the opening 44 may be formed as a hole of
which the periphery is surrounded. Moreover, in the present embodiment, one opening
44 is formed per one first blade part 43a, and a plurality of the openings may be
formed. Additionally, openings 44 may be formed in a lattice or in a net. In addition,
the driving force (drive torque) of the stirring impeller 4 can be further reduced
if a larger opening 44 is formed.
[0029] The blade unit 43 is disposed so as to incline to a downstream side in a rotational
direction with respect to the radial direction B of the support part 42. The angle
of such inclination to the downstream side, that is, an angle (receding angle) α at
which the inner peripheral side of the blade unit 43 retreats may be set to, for example,
10 degrees to 40 degrees. In addition, a configuration in which the blade unit 43
is not made to incline with respect to the radial direction may be adopted, or a configuration
in which the inner peripheral side of the blade unit 43 advances may be adopted.
[0030] Subsequently, the operation of the stirring device 1 including the stirring impeller
4 of the present embodiment will be described. First, if the driving unit 5 of the
stirring device 1 is driven to rotate the stirring shaft 3 in a direction (the counterclockwise
direction of Fig. 2(a)) in which a side where the first and second blade parts 43a
and 43b protrude inclinedly becomes a downstream side, the stirring impeller 4 rotates
together with the stirring shaft 3 around the stirring shaft 3 within the stirred
tank 2. If the stirring impeller 4 rotates, the liquid L and the gas G are mixed while
being sheared by the first blade part 43a and the second blade part 43b.
[0031] In a case where the stirring impeller 4 rotates in this way, the liquid L and the
gas G (objects to be stirred) pass through the opening 44 toward the upstream side
(rear side) from the downstream side (front side) in the rotational direction of the
blade unit 43. Additionally, after an object to be stirred in a gap portion S between
the first blade part 43a and the second blade part 43b, and the support part 42 has
moved to the opening 44 with a centrifugal force, this object to be stirred joins
the object to be stirred that passes through the above opening 44 and is dispersed
further to the outer peripheral side than the blade unit 43. As mentioned above, since
the objects to be stirred are made to join each other after the movement caused by
the centrifugal force, it is preferable that the opening 44 is formed in a predetermined
region on the radial outer side of the blade unit 43.
[0032] As above, the stirring impeller 4 of the present embodiment includes the support
part 42 and the blade unit 43. The blade unit 43 has the first blade part 43a, the
second blade part 43b, and the opening 44.
[0033] According to this configuration, as described above, cavitation is suppressed because
the blade unit 43 of the stirring impeller 4 has the opening 44. In addition, since
the driving force required for the driving of the stirring shaft 3 is reduced due
to such an improvement in stirring efficiency, it is also possible to make the stirring
shaft 3 relatively slim or and make the driving unit 5 relatively small. Additionally,
cost is also reduced. Additionally, operation at a lower torque and at higher-speed
rotation than ever before is also possible.
[0034] Additionally, in the present embodiment, the first blade part 43a and the second
blade part 43b are asymmetrically formed viewed in the radial direction. Moreover,
the first blade part 43a in one blade unit 43 of two blade units 43 adjacent to each
other in the circumferential direction is provided on the first surface 42a of the
support part 42, the first blade part 43a of the other blade unit 43 is provided on
the second surface 42b of the support part 42, the second blade part 43b of the one
blade unit 43 is provided on the second surface 42b of the support part 42, and the
second blade part 43b of the other blade unit 43 is provided on the first surface
42a of the support part 42. The opening 44 is formed in each first blade part 43a.
[0035] According to this configuration, even if a cavity is generated under the presence
of a large amount of gas, gas reservoirs (cavities) on back sides of the blade units
43 adjacent to each other are not easily combined. Accordingly, for example, in a
case where gas is present in large quantities in liquid, it is possible to suppress
a reduction of power and degradation of stirring performance.
[0036] Additionally, by providing the above configuration, the opening 44 is formed in an
upper first blade part 43a in one blade unit 43 of two blade units 43 adjacent to
each other, and the opening 44 is formed in a lower first blade part 43a of the other
blade unit 43. In this way, since the openings 44 are alternately arranged up and
down, it is possible to decentralize gas reservoirs generated near the blade units
43 in an upward-downward direction. Accordingly, flooding does not easily occur. The
flooding is a phenomenon in which the gas reservoirs adjacent to each other near the
blade units 43 are combined together and the function of the blade units 43 degrades
markedly.
[0037] Additionally, by alternately arranging the openings 44 up and down, it is possible
to decentralize the flow of a fluid without being centralized on one point. Accordingly,
velocity distribution in a heat transfer surface can be further equalized, and an
improvement in heat transfer performance is achieved. Additionally, in a case where
the invention is applied to an apparatus with high corrosiveness, induction of erosion
caused by the centralization of the flow of a fluid on one point can be prevented.
[0038] Next, since the inventor performed a performance test regarding the stirring impeller
4 of the present embodiment, test data is illustrated below.
[0039] The test conditions are as follows.
Test tank: transparent acrylics tank (internal diameter of tank: 310 mm, 2:1 semi-elliptical
bottom)
Impeller type: stirring impeller of the present embodiment, general-purpose (target
to be compared) disk turbine impeller diameter
Impeller diameter: 124 mm (impeller diameter ratio: 40%, refer to the following for
details)
Liquid type: water (density: 1000 kg/m3, viscosity: 1 cP) Water temperature: 12°C
Liquid volume: 26.1 L
Internal: baffle plate-four flat plates (width: 24.8 mm), one ventilation nozzle
Power: 1.0 kW/m3 (at the time of non-ventilation)
Number of rotations: stirring impeller of the present embodiment: 627 rpm (constant),
general-purpose disk turbine impeller: 350 rpm (constant)
Ventilation gas: ambient air in testing place Ventilation volume: 0 vvm to 3 vvm
[0040] The stirring impeller 4 of the present embodiment provided for the performance test
is made of stainless steel (SUS304), and has shapes illustrated in Fig. 2(a), Fig.2(b),
and Fig. 3. The sizes of main parts are as follows, and the positions of dimensions
(m1 to m7) of respective parts are illustrated in Fig. 4(a) and Fig. 4(b).
- Diameter of support part 42 (m1): 124 mm
- Plate thickness of support part 42 (m2): 2 mm
- Receding angle of first blade part 43a and second blade part 43b (α) : 30°
- Axial dimension from distal end of first blade part 43a to distal end of second blade
part 43b (m3): 22.5 mm
- Dimension between one-dot chain lines from root to distal end illustrated in Fig.
2 (b) in first blade part 43a and second blade part 43b (m4): 31.8 mm
- Curvature radius to surface of second blade part 43b on support part 42 side (m5):
49.2 mm
- Dimension along direction of receding angle α from outer peripheral edge of support
part 42 to radial-inner-side end edge of each of blade parts 43a and 43b (m6): 31.9
mm
- Dimension along direction of receding angle α from outer peripheral edge of support
part 42 to radial-inner-side end edge of opening 44 (m7): 13.5 mm
[0041] Additionally, a general-purpose disk turbine impeller used as a target to be compared
is an oblong plate-shaped disk in which the diameter of a disk having a disk shape
is 99 mm, and blades are arranged along a radial direction of the disk. In this turbine
impeller, six blades are arranged at regular intervals in a circumferential direction
of the disk, the diameter dimension of a blade tip is 124 mm, and each blade has a
vertical dimension of 25 mm and a horizontal dimension of 30 mm.
[0042] The performance test was performed by changing the ventilation volume from 0 vvm
to 3 vvm after the power at the time of non-ventilation was set to 1.0 kW/m3 in both
of the impellers. An upper graph illustrated in Fig. 5 is a graph illustrating the
relationship between the ventilation volume and kLa (overall mass transfer capacity
coefficient). kLa shows that more gas is dissolved in liquid as the numerical value
of kLa is larger. Additionally, a lower graph illustrated in Fig. 5 is a graph illustrating
the relationship between the ventilation volume and power (per unit volume of liquid)
transmitted to the liquid. As is clear from each graph, in a case where the ventilation
volume is the same, it is clear that the stirring impeller 4 (a line connecting circle
plots) of the present embodiment has larger kLa and the power transmitted to the liquid
is larger (that is, reduction of power is smaller), compared to the general-purpose
disk turbine impeller (a line connecting square plots on the graph) that is a target
to be compared.
[0043] From the above, it was proved by the performance test that the stirring impeller
4 of the present embodiment is superior to the general-purpose disk turbine impeller.
[0044] Although the stirring impeller 4 and the stirring device 1 related to the present
embodiment are as above, the stirring impeller and the stirring device related to
the invention are not limited to the above embodiment, and various changes can be
made without departing from the scope of the invention. Additionally, the effects
of the stirring impeller 4 and the stirring device 1 related to the invention are
not limited to the above-described effects.
[0045] In the above embodiment, an example in which six blade units 43 are provided at regular
intervals in the circumferential direction has been mentioned as the stirring impeller
4. However, the invention is not limited to this. In addition to this, the number
of blade units 43 may be appropriately set to, for example, 4 to 8 at regular intervals.
Additionally, the intervals between the blade units 43 may be appropriately set to
different intervals.
[0046] Additionally, in the above embodiment, an example in which the stirring shaft 3 and
the stirring impeller 4 rotate in the counterclockwise direction viewed from the top
part 23 side to the bottom part 22 side has been mentioned. In addition to this, however,
an aspect in which the stirring shaft 3 and the stirring impeller 4 rotate in the
clockwise direction may be adopted. In this case, flow reverse to that of the above
embodiment is obtained as the flow of an object to be stirred.
[0047] Additionally, applications to which the stirring impeller and the stirring device
related to the invention are applied are not particularly limited. For example, the
stirring impeller and the stirring device of the invention are used for a reaction
operation accompanied by the mass transfer of gas and liquid. As this reaction operation,
a gas absorption reaction operation in a hydrogenation reaction tank, an oxidation
reaction tank, or the like is mentioned. In addition, a reaction operation under the
presence of steam in a solvent removing agent reaction tank, a flash crystallization
reaction tank, or the like after rubber polymerization is mentioned. Moreover, the
stirring impeller and the stirring device of the invention are also used for a separation/extraction
operation.
[0048] The present embodiment is described together. The stirring impeller 4 related to
the present embodiment is the stirring impeller 4 attached to the stirring shaft 3
provided in the stirring device 1, and includes the plate-shaped support part 42 that
is attached to the stirring shaft 3, and the plurality of blade units 43 that are
disposed on the outer peripheral edge side of the support part 42, the support part
42 has the first surface and the second surface, and each of the blade units 43 includes
the first blade part 43a that protrudes from one of the first surface and the second
surface of the support part 42, the second blade part 43b that protrudes from the
other one of the first surface and the second surface in the support part 42 and is
made asymmetrical to the first blade part 43a, and the opening 44 that is formed in
at least one of the first blade part 43a and the second blade part 43b.
[0049] According to this configuration, after an object to be stirred in the gap portion
(S) between the first and second blade parts 43a and 43b and the support part 42 has
moved to the opening 44 with a centrifugal force, this object to be stirred joins
the object to be stirred that passes through the above opening 44 and is dispersed
further to the outer peripheral side than the blade unit 43. Since gathering and stagnation
in the object to be stirred in the gap portion between the first and second blade
parts 43a and 43b and the support part 42 are suppressed by virtue of such a flow
of the object to be stirred, cavitation can be suppressed. Since the resistance that
the blade unit 43 receives decreases as much as the object to be stirred passes through
the opening 44, the driving force of the stirring impeller 4 can be reduced.
[0050] Additionally, in the stirring impeller 4 of the above configuration, the support
part 42 may be formed in a circular shape, the plurality of blade units 43 may be
provided at predetermined intervals along the circumferential direction of the support
part 42, the first blade part 43a of one blade unit 43 of two blade units 43 and 43
adjacent to each other in the circumferential direction of the support part 42 may
be provided on the first surface of the support part 42, the first blade part 43a
of the other blade unit 43 may be provided of the second surface of the support part
42, the second blade part 43b of the one blade unit 43 may be provided on the second
surface of the support part 42, and the second blade part of the other blade unit
may be provided on the first surface of the support part.
[0051] According to this configuration, even if a cavity is generated under the presence
of a large amount of gas, gas reservoirs (cavities) on back sides of the blade units
43 and 43 adjacent to each other are not easily combined. As a result, for example,
in a case where gas is present in large quantities in liquid, it is possible to suppress
a reduction of power and degradation of stirring performance.
[0052] Additionally, regarding the first blade part 43a and the second blade part 43b that
are made asymmetrical to each other, for example, a configuration in which the first
blade part 43a is formed in a linear shape and the second blade part 43b is formed
in a curved shape may be adopted.
[0053] As described above, according to the present embodiment, the stirring impeller 4
with improved stirring efficiency and the stirring device 1 including the stirring
impeller 4 are provided.
Reference Signs List
[0054]
- 1:
- STIRRING DEVICE
- 2:
- STIRRED TANK
- 3:
- STIRRING SHAFT
- 4:
- STIRRING IMPELLER
- 41:
- BOSS PART
- 41a:
- THROUGH-HOLE
- 42:
- SUPPORT PART
- 43:
- BLADE UNIT
- 43a:
- FIRST BLADE PART
- 43b:
- SECOND BLADE PART
- 44:
- OPENING
- α:
- INCLINATION ANGLE
- L:
- LIQUID (OBJECT TO BE STIRRED)
- G:
- GAS (OBJECT TO BE STIRRED)
- A:
- AXIS CENTER DIRECTION
- B:
- RADIAL DIRECTION