[0001] The present invention relates to an agitator blade and a method of agitation using
said agitator blade, and more particularly to an agitator blade and an agitation method,
both being suitably applicable for extinguishing foam from foamable liquids, cleaning
of inner wall surface of agitating tank, effective utilization of heating surface
area, or mixing liquids of different specific gravities or liquids of different solid
contents.
[0002] In fermentation or culturing processes, the fermenting liquids and culturing liquids
are very prone to foam. Agitation foam causes foam during the process, and the foam
often impairs operability of the process. In order to inhibit such foaming and to
extinguish such foam, addition of anti-foaming agents such as silicone is generally
adopted. The use of such anti-foaming agents, however, not only requires significant
cost, but also poses a risk adversely affecting the fermentation and culturing processes,
because these anti-foaming agents are, in themselves, foreign substances to the liquids.
In addition, the anti-foaming agents are often included as impurities in the product
until the product is degraded. It requires additional labor to remove them from the
product. Furthermore, they contaminate waste liquid and impede a treatment of waste
liquid. Accordingly, addition of anti-foaming agents is not desirable and should be
controlled as little as possible.
[0003] Moreover, attempts have been made to carry out defoaming by a mechanical means which
is to suppress the foam by shearing force by rotating a disk in a foam layer on the
surface of the liquid or rotating a frusto-conical tube with allowing the lower opening
of the larger diameter to be in the foam layer. However, such means requires a great
power and besides, the foam is often merely subdivided and is not extinguished.
[0004] The inner wall surface of agitating tank is contaminated owing to microorganisms
or solid raw materials or products deposited thereon. This often causes decrease of
reaction yield or reduction of heat transfer coefficient.
[0005] In this case, it is substantially impossible to clean the inner wall surface of agitating
tank to remove the extraneous matters from the inner wall surface without stopping
the operation in the agitating tank.
[0006] When jackets, coiled hoses and calandrias are provided on the outer wall surface
and in the agitation tank as heating and cooling apparatuses, the liquid in the agitation
tank reduces, for example, by evaporation and liquid level lowers with lapse of time.
As a result, the heat transfer area of the heating and cooling apparatuses cannot
be effectively utilized.
[0007] Supply of fresh liquid is only the means to increase and recover the reduced heat
transfer area. However, supply of fresh liquid results in abrupt change of the composition
of the liquid and requires change in operational conditions and furthermore, quality
of product changes. Therefore, this means cannot be practically employed. Accordingly,
practially applicable means to solve the defect that the heat transfer area cannot
be effectively used has not yet been found.
[0008] Furthermore, mechanical rotational agitation using various agitator blades is carried
out in mixing liquids which differ in specific gravity and are hardly miscible and
mixing suspensions in which solid in the liquid settle to result in difference in
content of solid in upper and lower portions in the liquid in the tank. In this case,
however, a great power is required and in addition, there is the problem that the
mixing rate is not so high as expected for the great power required.
[0009] The inventors achieved the present invention after conducting elaborate researches
regarding agitation blades and methods of agitation, which, overcoming by mere mechanical
agitation the drawbacks in conventional defoaming by agitation and the drawbacks such
as contamination and reduction in heat transfer area of the inner wall surface of
agitation tank and the surface of heating and cooling apparatuses and low mixing rate
in mixing liquids of different specific gravity and suspensions, can efficiently and
thoroughly extinguish foam and can clean the inner wall surface of agitation tank
and the surface of heating and cooling apparatuses, can inhibit the reduction of heat
transfer area of the inner wall surface of agitation tank and heating and cooling
apparatuses, and can efficiently mix liquids of different specific gravities and suspensions.
[0010] Namely, the first invention lies in an agitating blade which is characterized by
one or more liquid transporting means arranged on a mounting frame attached to an
agitator shaft, the both ends of each of said liquid transporting means being opened
to have an upper opening and a lower opening, respectively.
[0011] The second invention is an agitating method. In agitation of foamable liquid and
unfoamable liquid, the method is characterized by arranging one or more liquid transporting
means on a mounting frame attached to an agitator shaft, forming upper openings and
lower openings at the both ends of said liquid transporting means of the agitator
blade, locating the upper openings and the lower openings in the space above the liquid
surface and in the liquid in an agitation tank, respectively, and rotating said agitator
blade to agitate the liquid and simultaneously discharge the liquid in the tank from
the upper openings into the space above the surface of the liquid in the tank through
said liquid transporting means.
[0012] The third invention is a method of agitating and mixing liquids. The method is characterized
by arranging one or more liquid transporting means on a mounting frame attached to
an agitator shaft, forming upper openings and lower openings at the both ends of each
of said liquid transporting means of an agitator blade, interconnecting the upper
part and the lower part of the liquid in an agitation tank by said liquid transporting
means, and rotating the agitator blade to discharge one of the liquids from openings
of the liquid transporting means into another liquid, thereby to mix the upper liquid
and the lower liquid.
[0013]
Fig. 1 is a plan view of the agitator blade of the present invention.
Fig. 2 is a side view of the agitator blade of the present invention.
Fig. 3 is a longitudinal sectional view of an agitation tank in which the agitator
blade shown in Figs. 1 and 2 is used.
Fig. 4 is a plan view of the mounting frame of the agitator blade of the present invention.
Fig. 5 shows a spray shower type tube body which is the liquid transporting means
of the present invention and (a) and (b) are aside view and a plan view, respectively.
Fig. 6 shows a spray shower type tube body which is the liquid transporting means
of the present invention, and (a) and (b) are a side view and a underside view, respectively.
Fig. 7 shows a spray shower type tube body which is the liquid transporting means
of the present invention, and (a) and (b) are a side view and a underside view, respectively.
Fig. 8 shows a spray type tube body which is the liquid transporting means of the
present invention, and (a) and (b) are a side view and a bottom view, respectively.
Fig. 9 shows a gutter body which is the liquid transporting means of the present invention,
and
(a), (b) and (c) are an oblique view, a side view and a plan view, respectively.
Fig. 10 shows a plate body which is the liquid transporting means of the present invention
and (a), (b) and (c) are an oblique view, a side view and a plan view, respectively
and (d) and (e) are an oblique view and a plan view of a modified plate body, respectively.
Fig. 11 shows the agitator blade of the present invention attached slidably to the
agitator shaft, and (a) is a plan view and (b) is a sectional view taken along the
line A-A.
Fig. 12 shows the agitator blade of the present invention where the tube body which
is the liquid transporting means is attached to the agitation shaft through a mounting
frame at an angle of 0 to the radial direction of the rotating plane, and (a) is a
plan view of the agitator blade and (b) is a sectional view of the agitator blade
shown in (a), taken along the line B-B.
Fig. 13 shows the agitator blade of the present invention where the liquid transporting
means is a hollow truncated cone body, and (a) is a plan view of the agitator blade
and (b) is a sectional view of the agitator blade shown in a, taken along the line
C-C.
Fig. 14 shows the agitator blade of the present invention where the liquid transporting
means comprises two hollow truncated cone bodies, and (a) is a plan view of the agitator
blade and (b) is a sectional view of the agitator blade shown in (a), taken along
the line D-D.
[0014] In the present invention, "upper" and "lower" mean "a position near the bottom of
liquid" and "a position far from the bottom", respectively.
[0015] The mounting frame is designed to mount the agitator blade on an agitator shaft and
to hold one or more liquid transporting means. The mounting frame may be formed of
either rods, square bars, shaped steels, plates provided with many perforations (sometimes
referred to as perforated plates hereinafter) or non-perforated plates. These non-perforated
plates and perforated plates are preferably provided at the agitator shaft so as to
reduce fluid resistance as much as possible when rotated in liquid. The non-perforated
plates is preferably those which have a narrow width when they are used in longitudinal
state (in the state perpendicular to rotating plane of the agitator blade).
[0016] These rods, square bars, shaped steels, perforated plates and non-perforated plates
are positioned approximately on the diameter line of the rotating plane. The number
of these rods, square bars, shaped steels, perforated plates and non-perforated plates
may be one or more. When plural numbers are used, each member may be positioned either
on the same rotating plane or on the plane differing each other.
[0017] These mounting frames are arranged approximately perpendicular to the agitator shaft.
[0018] When a plurality of the liquid transporting means are used, their intervals are appropriately
selected depending on viscosity of liquid, size of the liquid transporting means,
diameter of an agitation tank body, and angle between the rotating axis and the liquid
tranporting means.
[0019] The liquid transporting means may be ones through which liquid can move and are usually
tube bodies, but may be gutter bodies, plate bodies and bottomless and hollow truncated
cone bodies.
[0020] The tube body can be a straight tube as a whole, but may have an upper portion formed
straight and a lower portion formed bent or may be nearly S shaped. It is preferred
in practice that the bent portion be fixed approximately perpendicular to the rotating
axis or slightly inclined downward with respect thereto. Furthermore, the upper strainght
portion may be preferably directed to obliquely upper or lower direction or to side
wall of the agitation tank, or may be bent to optional directions such as toward the
rotating axis.
[0021] The lower bent portion of tube body may be formed either by bending the lower portion
or by connecting a separate tube to the end of the straight portion, for example,
by welding or screwing.
[0022] The bent portion of the tube body is preferably formed, on the rotating plane containing
the junction point between the bent and straight portions, at an angle of substantially
0-90
° to radial direction of the rotating plane, namely, on the radius of the rotating plane
or along a circle drawn with a radius equal to the distance from the rotating axis
to said junction point, or along the tangent line to the above circle. Alternatively,
the whole tube body can be curved along an arc of a circle having a radius nearly
equal to the distance from the agitation shaft to the position at which the tube body
is fixed. Moreover, it is also possible to form the whole tube body straight viewing
from upper or lower side of the rotating plane and to arrange the tube body on the
mounting frame at an angle of substantially 0-90
° to the radial direction of rotating plane as mentioned above.
[0023] The same can be applied to the liquid trnasport means in the form of gutter body
and plate body.
[0024] The upper and lower ends of the tube body are opened in the agitation tank to form
an upper opening and a lower opening, respectively. When a plurality of the tube bodies
are provided, the fellow upper openings and the fellow lower openings may respectively
be located either on substantially the same rotating plane or on different planes.
[0025] Shape of the upper opening of the tube body is unlimited and usually circular form
such as circle, ellipse or oval or polygon such as triangle, square, rectangle, rhombus,
hexagon or octagon.
[0026] The upper opening can be covered with a perforated plate and, if necessary, this
upper opening can be in the form of funnel and thus, the tube body can be shower spray
type tube body.
[0027] The spray type tube body can also be formed by using a blind tube with no opening
as the upper opening portion and perforating many holes therethrough.
[0028] Shape of the lower opening of the tube body and that of section of the tube body
are also unlimited and usually circular form such as circle, ellipse or oval or polygon
such as triangle, square, rectangle, rhombus, hexagon or octagon.
[0029] The gutter body as liquid transporting means corresponds to the above-mentioned tube
body from which the upper part is cut away, and shapes of section and upper and lower
openings are, for example, half circle, half ellipse, half oval, U-shape and V-shape,
and polygon such as square or rectangle from which one side is omitted.
[0030] The plate body as liquid transporting means has a whole side shape such as linear
shape or long S shape and has a whole planar shape such as long trapezoid or rectangle
or either of these shapes curved at a small curveture. One of the both ends of this
plate body which is allowed to go ahead may be upwardly or downwardly twisted so that
the outer periphery side (in use of the agitator) is directed to the mounting frame.
[0031] The upper end and the lower end of the plate body as the liquid transporting means
correspond to the upper opening and the lower opening, respectively.
[0032] The shape of upper opening and that of lower opening of the liquid transporting means
such as tube body, gutter body and plate body (sometimes referred to as long and narrow
liquid transporting means hereiafter) may be the same or different.
[0033] One of the both openings of the long and narrow liquid transporting means which is
allowed to go advance at the time of agitation may be thin and sharp in its end to
reduce fluid resistance.
[0034] The area of the upper opening and the lower opening of the long and narrow liquid
transporting means may be either substantially equal or different, the latter being
preferred for practical use. In the latter case, the ratio of the both openings is
optionally selected depending on the kind of the liquid, purpose of agitation and
operational conditions.
[0035] Furthermore, in the latter case, either of the openings can be an opening which scoops
up the liquid (sometimes referred to as intake opening hereiafter) or an opening which
discharges the liquid (sometimes referred to as discharge opening hereinafter), but
for practical use the larger opening is normally employed as the intake opening.
[0036] Here, in the case of the opening covered with a perforated plate or the opening comprising
many holes, the area of opening is total area of the holes.
[0037] As for the liquid transporting means of gutter body and plate body, when the top
opening is linear or curved, the length of the line and that of the curve correspond
to the area of the openings.
[0038] When this agitator blade is used for defoaming, the upper opening is preferably in
the form substantially parallel to the mounting frame, namely, flat shape substantially
parallel to the rotating plane, for instance, long rectangular, rhombus, oval or ellipse.
Preferably, the upper opening is not covered with a perforated plate and completely
opened.
[0039] The long and narrow liquid transporting means are arranged either perpendicular or
inclined to the mounting frame. In operation, the liquid transporting means become
almost parallel to the rotating axis in the former case, while inclined in the latter
case. In practice, the inclined arrangement is preferred.
[0040] The long and narrow liquid transporting means are usually arranged so that the intake
opening is allowed to go ahead in rotation of the agitator. When a plurality of the
long and narrow liquid transporting means are arranged inclined, the angles of inclination
may be the same or different.
[0041] When the inclined arrangement is adopted, the angle of inclination of the long and
narrow liquid transporting means (the angle between the rotating axis and the long
and narrow liquid transporting means) may vary depending on the viscosity of the liquid,
the size of the long and narrow liquid transporting means, etc. and is not able to
be generally fixed to a given angle. The range from about 15-75
° is preferable in practice.
[0042] A plurality of long and narrow liquid transporting means arranged on the mounting
frame are generally same in size, shape and type, but may be different.
[0043] The long and narrow liquid transporting means can be rotatably attached to the mounting
frame so as to be able to freely adjust the angle to the rotating axis and the angle
to the radial direction of rotating plane.
[0044] In case the long and narrow liquid transporting means is a bottomless and hollow
truncated cone body (sometimes referred to as hollow truncated cone body hereinafter),
this hollow truncated cone body is attached to the agitation shaft through the mounting
frame with allowing the longer aixis to substantially coincide with the longer aixis
of the agitating axis.
[0045] One hollow truncated cone body may be used as the liquid transporting means. Alternatively,
a plurality of hollow truncated cone bodies differing in diameter may be cocentrically
arranged. Moreover, a baffle may be provided at the inner wall surface of the hollow
truncated cone body along the slant of the wall or in the inclined direction.
[0046] In the case of liquid transporting means of hollow truncated cone body, the opening
corresponding to the bottom of the truncated cone is the opening of the liquid transporting
means.
[0047] The space formed by side walls of a plurality of the hollow truncated cone bodies
is a channel of liquid when the hollow truncated cone bodies are rotated.
[0048] The hollow truncated cone body is used in the truncated cone form or reverse truncated
cone form by using the opening of smaller diameter as upper or lower opening depending
on the purposes of use.
[0049] In this hollow truncated cone body, the opening of smaller diameter and the opening
of larger diameter are respectively the intake opening and the discharge opening irrespective
of rotating direction in use of the agitator blade.
[0050] In the present invention, the liquid in the agitation tank is transferred through
the liquid transporting means according to Bernoulli's theorem and/or centrifugal
force by rotating the liquid transporting means.
[0051] The agitator blade of the present invention is rigidly fixed to the agitator shaft
by means of the mounting frame or slidably fitted to the shaft.
[0052] Any fixing may be employed, for example, sealing, screwing, welding or bonding.
[0053] For slidably fitting the agitator blade, for example, grooves, projections or projected
lines are provided on the surface of the agitator shaft along the longer axis and
projections, projected lines or grooves which can be fitted with said grooves, projections
or projected lines to slide the agitator blade are provided on the mounting frame.
[0054] The mounting frame slidably fitted to the agitator shaft can be automatically or
manually moved. For example, floats are provided at the mounting frame and floated
on the surface of liquid so that the mounting frame can be moved in correspondence
to the rising and falling of the surface of liquid in the tank. Alternatively, the
mounting frame can be moved up and down by remote handling outside the tank and stopped
at a desired position. The mounting frame can be manually moved up and down by suspending
the mounting frame by a wire connected to outside and stretching or relaxing the wire
outside the tank.
[0055] The above floats can also serve as the mounting frame. The floats preferably have
such a shape and structure as reducing fluid resistance as much as possible in agitation.
[0056] This agitator blade is usually rotated so as to allow the intake opening to go ahead
in operation when a long and narrow liquid transporting means is used.
[0057] In the agitation method of the present invention, the rotating speed of the agitator
blade is adequately selected according to kinds of liquid, the degree of foamability
and the degree of foaming, preferably not smaller than about 2.5 m/sec as a speed
of the tip of the blade in practice.
[0058] In the agitation method of the present invention, in order to discharge the liquid
in the tank from the upper opening of the long and narrow liquid transporting means
into the space above the surface of liquid, when said long and narrow liquid transporting
means is provided, for example, at substantially 90
° to the radius of rotating plane, the upper opening and the lower opening are located
in the space above the surface of liquid and in the liquid in the agitation tank,
respectively and the agitator blade is rotated with allowing the lower opening to
go ahead to scoop up the liquid in the tank from the lower opening of the liquid transporting
means, thereby to discharge the liquid from the upper opening of the liquid transporting
means.
[0059] When the long and narrow liquid transporting means is provided, for example, at 0
to the radius of rotating plane, the opening on circumferential side of the rotating
plane is exposed above the surface of liquid and is used as an upper opening. Thus,
irrespective of whether the long and narrow liquid transporting means is rotated clockwise
or counterclockwise in respect to the rotating axis, the liquid in the tank can be
scoop up into the liquid transporting means from the lower opening on the central
side of the rotating plane and can be discharged from the upper opening into the space
above the surface of the liquid.
[0060] When the liquid transporting means is a hollow truncated cone body, this can be used
in the form of reverse truncated cone and the opening of larger diameter may be exposed
from the surface of liquid as an upper opening. The liquid discharged from this upper
opening is sprayed over the surface of foam layer in order to carry out defoaming.
[0061] Furthermore, the liquid discharged from the upper opening is sprayed to the inner
wall surface of the agitation tank and to the surface of heating- cooling apparatuses
and is allowed to fall along these surfaces whereby the inner wall surface of the
tank and the surface of heating cooling apparatuses are cleaned and the heat transfer
area can be effectively used. This method is usually applied to unfoamable liquid,
but can also be applied to foamable liquid.
[0062] It is also possible to use for defoaming the liquid discharged from the upper openings
of a part of a plurality of the long and narrow liquid transporting means and to use
the liquid discharged from the upper openings of the other liquid transporting means
for cleaning of the inner wall surface of the tank and the surface of heating cooling
apparatuses and increasing the heat transfer area.
[0063] When the agitator blade of the present invention is used to agitate and mix liquids,
the upper openings and the lower openings of the long and narrow liquid transporting
means are located in the upper part and the lower part of the liquid in the tank,
respectively and both the upper and lower parts of the liquid in the tank are interconnected
through the liquid transporting means. When the agitator blade is rotated so as to
allow the upper openings to go ahead, the upper liquid falls through the liquid transporting
means and is discharged into the lower liquid from the lower openings. When the agitator
blade is rotated so as to allow the lower openings to go ahead, the lower liquid rises
through the liquid transporting means and is discharged into the upper liquid from
the upper openings. As a result, both the liquids are mixed.
[0064] When the long and narrow liquid transporting means is provided, for example, at 0
to the radius of rotating plane, irrespective of the direction of rotation, the opening
on the circumferential side of the rotating plane and the opening near the center
of the rotating plane are intake opening and discharge opening, respectively.
[0065] In the case of the liquid transporting means being a hollow truncated cone body,
irrespective of the rotating direction, the opening of smaller diameter is intake
opening and the opening of larger diameter is discharge opening. Accordingly, when
the hollow truncated cone body is used in the form of truncated cone in the agitation
tank, the liquid is allowed to fall through the liquid transporting means which is
a hollow truncated cone body, and when the hollow truncated cone body is used in the
form of reverse truncated cone, the liquid is allowed to rise through the liquid transporting
means which is a hollow truncated cone body.
[0066] For this agitation and mixing, it is preferred to select tube bodies as the long
and narrow liquid transporting means.
[0067] The liquids to be mixed include suspensions and immiscible liquids differing in specific
gravity. The upper part and the lower part of the liquid in the agitation tank are
liquid of smaller specific gravity and that of larger specific gravity, respectively.
The suspensions are those which are formed due to settling of solids during agitation.
[0068] The agitator blade of the present invention may be used in combination with conventional
agitation blades such as turbine blades, propellers, angled flat vanes, pitched flat
vanes, flat vane disk turbines, flat vanes, curved vanes, or Faudola vanes and Bulmargin
vanes, as well as other agitating means such as agitation by jetting and/or ventilating
agitation. The combination is preferable.
[0069] The mounting frame per se can be served as agitator blade.
[0070] The present invention will be explained in concrete by the examples referring to
the drawings, but it is not limited thereto.
Fig. 1 and Fig. 2 are a plan view and a side view of the agitator blade of the present
invention which is fixed to an agitator shaft.
Fig. 3 is a longitudinal sectional view of an agitation tank where the agitator blade
shown in Figs. 1 and 2 is used.
Fig. 4 is a plan view of the mounting frame for the agitator blade of the present
invention.
Figs. 5-10 show various embodiments of liquid transporting means.
Fig. 11 is a plan view of the agitator blade of the present invention slidably fitted
to an agitation shaft and a sectional view of the agitator blade taken along the line
A-A.
[0071] The agitator blade 1 includes a mounting frame 11 and a tube body 12 which is a liquid
transporting means. A non-perforated plate of narrow width is used as the mounting
frame 11. A total of six tube bodies 12 which are the liquid transporting means are
provided, three on each side of the mounting frame 11. These tube bodies 12, 12, ----12
are arranged tilting on the mounting frame 11, and inclined to the agitation shaft
2 (rotating axis) at the time of running. Angle of inclination is about 30
°.
[0072] The tube body 12 consists of an upper straight portion 121 and a lower bent portion
122. The tube body 12 is formed here by screwing the bent portion 122 to the bottom
end of the straight portion 121 at the junction point 123. The bent portion 122 is
formed at an angle of 90 to the radial direction at rotating plane of the junction
point 123, namely, formed to go along the tangent line to a circle drawn on the rotation
plane of the junction point 123 with a radius equal to the distance between the junction
point 123 and the agitating axis (the center of the rotating plane). The bent portion
122 is attached almost perpendicular (almost parallel to the rotating plane) to the
rotating axis (agitator shaft 2).
[0073] The ends of the straight portion 121 and the bent portion 122 are opened in the agitation
tank to form an upper opening 124 and a lower opening 125, respectively.
[0074] The fellow upper openings 124, 124, n---, 124 and the fellow lower openings 125,
125, n---, 125 are arranged to open on substantially the same rotating plane, respectively.
[0075] The shape of the upper openings 124, 124, n---, 124 is a flat rectangular form substantially
parallel to the mounting frame 11 or the rotating plane, while the shape of the lower
openings 125, 125, -----, 125 is substantially circular.
[0076] The opening direction of the upper openings 124 and the lower openings 125 are upwardly
inclined and horizontal, respectively.
[0077] The area of the upper opening 124 is smaller than that of the lower opening 125.
[0078] The agitator blade 1 is installed in the agitation tank 3 by fixing the mounting
frame 11 with its center to the agitator shaft 2, the frame 11 becoming almost perpendicular
to the agitator shaft 2.
[0079] The agitation tank 3 includes a cylindrical tank body 31, the center of the top plate
of which is penetrated by the agitator shaft 2, the point of the penetration being
sealed by a shaft seal 32. The lower end of the agitator shaft 2 is borne by a bearing
33 at the bottom of the tank body 31. The bottom plate and the bottom plate of the
tank body 31 are provided with a gas inlet 34 and a liquid outlet 35 and a gas outlet
36, respectively. A pipe is extended from the gas inlet 34 to the inner bottom of
the tank body 31, its end portion being provided with a ring gas distributor 37 drilled
of many holes, while at the middle of the pipe said bearing 33 being mounted. The
agitator shaft 2 is connected to a motor 4 at its top end. The agitator shaft 2 has
three turbine blades 5, 5, 5 mounted thereon below the agitator blade 1.
[0080] In order to carry out defoaming, for example, in the surface portion of the liquid
in the agitation tank 3 by discharging the liquid from the upper opening 124 of the
tube body 12 of the agitator blade 1 into the space above the surface of the liquid,
the upper opening 124 and the lower opening 125 of the tube body 12 are located in
the space above the foam layer 6 on the surface of the liquid and in the unfoamed
liquid 7 under the foam layer and the agitator blade 1 is rotated with allowing the
lower opening 125 to go ahead (clockwise in Fig. 1) to scoop up the liquid from the
lower opening 125 and this liquid is allowed to rise through the liquid transporting
means 12 and discharged from the upper opening 124, and sprayed on the surface of
the foam layer 6 to smash the foam to carry out defoaming.
[0081] The liquid thus discharged from the upper opening 124 is sprayed onto the inner wall
surface of the tank body 31 and is dropped along the inner wall surface whereby the
inner wall surface of the tank body 31 is cleaned and the heat transfer area is effectively
used.
[0082] As other possible forms of the mounting frame 11, two frames such as perforated plate
bodies of narrow width can be crossed at right angles on the same rotation plane on
a plan view as shown in (a) of Fig. 4. Alternatively, the frame may be perforated
disk as shown in (b) of Fig. 4.
[0083] The mounting frame shown here is fitted to the agitator shaft so that its plane is
substantially parallel to the rotating plane of the agitator blade.
[0084] Figs. 5-7 show spray shower type tube bodies which are liquid transporting means.
[0085] Fig. 8 shows a spray type tube body.
(a) in Figs. 5-8 is a side view of the tube body.
(b) in Fig. 5 is a plan view.
(b) in Figs. 6-8 is a bottom view.
[0086] The tube portion 126 of the tube body 12 shown in Fig. 5 is curved upwardly viewing
from the side and is also slightly curved viewing from above. The top end of the tube
portion 126 is in the form of a funnel, namely, forms a funnel portion 127. The upper
opening 124 is in the rectangular form and is covered with a perforated plate. The
shape of the lower opening 125 is circular. The opening directions of the upper opening
124 and the lower opening 125 are inclined upwardly and horizontal, respectively.
[0087] The tube portion 126 of the tube body 12 shown in Fig. 6 is in the form of long S
viewing from the side and the top end thereof is bent in downwardly inclined direction
and is curved at a small curveture seeing from below. The top end of the tube portion
126 is in the form of a funnel, namely, forms a funnel portion 127. The upper opening
124 is in the form of ellipse and is covered with a perforated plate. The shape of
the lower opening 125 is circular. The opening directions of the upper opening 124
and the lower opening 125 are downwardly inclined and horizontal, respectively.
[0088] The tube portion 126 of the tube body 12 shown in Fig. 7 is in the form of long S
viewing from the side and is slightly curved seeing from below. The top end of the
tube portion 126 is in the form of a funnel, namely, forms a funnel portion 127. The
upper opening 124 is in the form of circle and is covered with a perforated plate.
The shape of the lower opening 125 is circular. The opening directions of the upper
opening 124 and the lower opening 125 are side direction far off from the agitator
shaft and horizontal direction, respectively.
[0089] The tube portion 126 of the tube body 12 shown in Fig. 8 is in the form of flat S
viewing from the side and the lower end is curved at a small curveture seeing from
below. The direction of the curving is such as the lower opening 125 coming near the
rotating axis when fitted to the mounting frame.
[0090] The top end of the tube portion 126 is closed to form a blind tube. Many holes are
drilled at the underside of the top end portion of the tube portion 126 to form the
upper opening 124. The shape of the lower opening 125 is circular. The opening direction
of the lower opening 125 is horizontal.
[0091] In the liquid transporting means shown in Figs. 5-8, the lower part of the tube body
is thicker than the upper part and the opening area of the lower opening is larger
than that of the upper opening.
[0092] Fig. 9 shows gutter body 8 as the liquid transporting means.
[0093] (a), (b) and (c) in Fig. 9 are an oblique view, a side view and a front view of the
gutter body 8.
[0094] The gutter body 8 shown in Fig. 9 is in the form of a long and nearly half hollow
truncated cone with no bottom. The shape of the upper opening 81 and that of the lower
opening 82 are both semicircular. Planar shape is long trapezoid and the lower portion
is slightly curved. The curving direction is such that the lower opening 82 comes
close to the rotating axis when fitted to the mounting frame.
[0095] In the liquid transporting means shown in Fig. 9, area of the lower opening is larger
than that of the upper opening. The area of opening of these liquid transporting means
is a length of the arc of the semicircle of the upper and lower end openings.
[0096] Fig. 10 shows a plate body 9 as the liquid transporting means.
[0097] In Fig. 10, (a), (b) and (c) show an oblique view, a side view and a front view of
the plate body; (d) and (e) show modifications of the plate body shown in (a)-(c)
and are an oblique view and a front view, respectively.
[0098] The whole side shape of the plate body 9 shown in (a)-(c) of Fig. 10 is a long S
and the whole planar shape is a long trapezoid.
[0099]
(d) shows a plate body 91 which is upwardly bent at the lower end corner 911 (the
right end in (d) which is allowed to go behind at the time of rotating).
(e) shows a plate body 92 having a whole front shape of long trapezoid curved at a
small curveture.
[0100] In the liquid transporting means shown in Fig. 10, area of the lower opening is larger
than that of the upper opening. The area of opening of these liquid transporting means
is a length of the straight line of the upper end opening and is defined to be a length
of the straight line or the curve of the lower end opening.
[0101] Fig. 11 shows an agitator blade provided with float 10 which also serves as a mounting
frame and slidably fitted to an agitator shaft.
[0102] In Fig. 11, (a) and (b) are a plan view of the agitator blade and a sectional view
of the agitator blade taken along the line A-A.
[0103] The floats 10, 10 are ring-shaped and have a section of nearly square and these are
a float of larger diameter and a float of smaller diameter which are concentrically
positioned on the same rotating plane. A plurality of tube bodies 12, 12, n---, 12
are fixed to the inner circumferential side face of the floats 10, 10 by fixers 101,
101, ---, 101 (in Fig. 11, each two of four tube bodies 12, 12, 12, 12 are fixed to
the floats 10, 10 on the same diameter symmetrically with respect to the rotating
axis as an axis of symmetry and the agitator blade is omitted). The floats 10, 10
are connected by a central ring 102 provided at the center and supporting rods 103,
103. These supporting rods 103, 103 cross each other at right angles. A protrusion
104 is provided at the inner peripheral face of the central ring 102. A groove 21
is cut on the outer peripheral face of the agitator shaft 2 along its longer axis.
The agitator blade 1 can be slidably attached to the agitator shaft 2 by inserting
the agitator shaft 2 through the central ring 102 and fitting the groove 21 of the
agitator shaft with the protrusion 104.
[0104] Fig. 12 shows the agitator blade of the present invention comprising an agitator
shaft to which tube bodies are fitted at an angle of 0 to the radial direction of
rotating plane by the mounting frame. (a) in Fig. 12 shows a plan view of the agitator
blade and (b) shows a sectional view of the agitator blade shown in (a) taken along
the line B-B. The tube body 12 is attached to the top end of the mounting frame 11
at an inclinaton angle of about 45 to the rotating axis 2. The tube 12 is provided
at substantially 0
° to the radial direction of its rotating plane, namely, on the radius of the rotating
plane. The four mounting frames 11, 11, 11, 11 provided with the tube bodies 12 are
arranged on the outer periphery of the central ring 102 at a center angle of 90
°. The tube body 12 is an almost straight cylinder. The upper end is nearly horizontally
bent and the top end is flattened in horizontal direction. The shape of the lower
opening is circle. The agitator shaft 2 is inserted through the central ring 102.
[0105] In this agitator blade, the upper opening 124 and the lower opening 125 of the tube
body 12 are respectively a dicharge opening and and intake opening irrespective of
the direction of rotating direction of the agitator blade.
[0106] Figs. 13 and 14 show the agitator blades of the present invention where the liquid
transporting means are hollow truncated cone bodies. (a) in Fig. 13 shows a plan view
of the agitator blade and (b) shows a sectional view of the agitator blade taken along
C-C.
[0107] (a) in Fig. 14 shows a plan view of the agitator blade and (b) shows a sectional
view of the agitator blade taken along D-D.
[0108] In this agitator blade shown in Fig. 13, the hollow truncated cone body 201 is the
liquid transporting means which is attached to the agitator shaft 2 with the longer
axis thereof being allowed to nearly coincide with the longer axis of the agitator
shaft 2. Four baffles 203, 203, 203, 203 are provided at equal intervals on the inner
peripheral face of this hollow truncated cone body along the inclination of the inner
peripheral face.
[0109] This hollow truncated cone body 201 is in the form of a reverse truncated cone with
the larger opening being an upper opening and arranged on the central ring 102 through
mounting frame 11. Through this central ring 102 is inserted the agitator shaft 2.
[0110] In this hollow truncated cone body 201, the lower opening 204 of smaller diameter
and the upper opening 205 of larger diameter are respectively an intake opening and
a discharge opening irrespective of its rotating direction.
[0111] The liquid in the agitation tank is scooped up from the lower opening 204 as an intake
opening and is allowed to rise along the inner peripheral face of this hollow truncated
cone body 201 and discharged from the lower opening 205 as a discharge opening by
rotating the agitator blade.
[0112] The agitator blade shown in Fig. 14 is substantially not different from the agitator
blade shown in Fig. 13 except that a hollow truncated cone body 202 having a smaller
diameter than that of the hollow truncated cone body 201 and equal in gradient of
peripheral wall to the hollow truncated cone body 201 is concentrically provided in
the hollow truncated cone body 201, no baffles are provided on the inner peripheral
faces of the hollow truncated cone bodies 201 and 202, and the liquid in the agitation
tank is allowed to rise through the space 206 between the hollow truncated cone bodies
201 and 202 and along the inner peripheral face of the hollow truncated cone body
202.
Example of use
[0113] The agitation tank shown in Fig. 3 was used as a fermentation equipment.
[0114] In this equipment, when a customarily employed turbine blade was used in place of
the agitator blade of the present invention, defoaming was not able to be performed
only by the agitation machine using the turbine blade and when a defoamer was additionally
used, the cost for silicone used as the defoamer for completely extinguishing foam
was about 70,000 yen per day.
[0115] The use of the agitator blade of the present invention facilitated thorough defoamation
without any defoaming agent. There was no substantial difference in power required
over a case where no agitator blade of the present invention was used.
[0116] The agitator blade and the method of agitation using this agitator blade of the present
invention makes it possible to completely defoam without any defoaming agent in agitation
of foamable liquids. There is no difficulty encountered in fermentation and culturing.
No defoaming agents are left unremoved as impurity in the product. High quality of
the product is secured. No additional labor is required in order to remove the defoaming
agent from the product. A treatment of waste liquid is effected without any difficulty.
[0117] Furthermore, the inner peripheral face of the agitation tank and the surface of heating
cooling apparatuses can be cleaned and the heating surface area can be effectively
used without stopping the operation in the agitation tank. Efficient mixing of liquids
having different specific gravities and differing in solid content is also possible.