U.S. patent number 3,690,621 [Application Number 04/804,743] was granted by the patent office on 1972-09-12 for agitator.
This patent grant is currently assigned to Kyowa Hakko-Kogyo Co., Ltd.. Invention is credited to Tadashi Hirotani, Masatami Tanaka, deceased.
United States Patent |
3,690,621 |
Tanaka, deceased , et
al. |
September 12, 1972 |
AGITATOR
Abstract
The present disclosure is directed to an agitating apparatus
comprising an agitating blade assembly, said agitating blade
assembly including upper and lower disk means which are spaced
apart by a plurality of radially disposed plate means, said lower
disk means also containing a plurality of radially disposed blade
plate means attached to its bottom side, and agitating shaft means
extending through an opening in the upper disk means and attached
to the top side of the lower disk means.
Inventors: |
Tanaka, deceased; Masatami
(LATE OF Machida-shi, Tokyo, JA), Hirotani; Tadashi
(Tokyo, JA) |
Assignee: |
Kyowa Hakko-Kogyo Co., Ltd.
(Tokyo, JA)
|
Family
ID: |
25189715 |
Appl.
No.: |
04/804,743 |
Filed: |
March 4, 1969 |
Current U.S.
Class: |
366/265; 416/184;
261/84 |
Current CPC
Class: |
B01F
7/00241 (20130101); B01F 2005/0011 (20130101); B01F
7/0015 (20130101); B01F 7/00583 (20130101) |
Current International
Class: |
B01F
15/00 (20060101); B01F 7/00 (20060101); B01F
5/00 (20060101); B01f 005/16 () |
Field of
Search: |
;259/111,102,96,95
;416/182,184,185,186 ;261/84,93,32 ;230/134.48 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
|
|
|
|
|
|
|
1,474,582 |
|
Feb 1967 |
|
FR |
|
552,573 |
|
Apr 1943 |
|
GB |
|
Primary Examiner: Scheel; Walter A.
Assistant Examiner: Cantor; Alan I.
Claims
What is claimed is:
1. An agitating apparatus comprising an agitating blade assembly,
said agitating blade assembly including upper and lower flat
horizontal circular disk means which are parallel to one another
and which are spaced apart by a plurality of radially extending
curved plate means, said upper disk means being provided with a
centrally disposed opening, a plurality of radially extending flat
blade plate means attached to the bottom side of the lower disk
means, the flat blade plate means having horizontal bottom edges
which are parallel to said lower disk means, and agitating shaft
means extending through the centrally disposed opening and secured
to the top side of the lower disk means.
2. An agitating apparatus comprising an agitating blade assembly,
said agitating blade assembly including upper and lower circular
disk means which are spaced apart by a plurality of radially
extending curved plate means, said upper disk means being provided
with a centrally disposed opening, a plurality of radially
extending flat blade plate means attached to the bottom side of the
lower disk means and agitating shaft means extending through the
centrally disposed opening and secured to the top side of the lower
disk means, wherein the curved plate means extend into the
centrally disposed opening.
3. The apparatus of claim 2, wherein the curved plate means are
tapered to a point extending from the periphery of the opening into
said opening.
4. The apparatus of claim 2, wherein the curved plate means extend
from the periphery of the disc means into the centrally disposed
opening.
5. The apparatus of claim 2, wherein the flat blade plate means
extend inwardly from the periphery of the lower disk means to a
position spaced from the center of said disk means.
6. An aeration-agitating apparatus comprising a plurality of
radially extending flat blade means attached to the underside of a
lower flat horizontal circular disk means, said flat blade means
having lower horizontal edges which are parallel to said lower disk
means, a plurality of substantially radially extending curved blade
means attached at their bottoms to the upper side of said lower
disk means, an upper flat horizontal circular disk means attached
at the bottom side thereof to the tops of said curved blade means,
and connecting means for connecting at least one of said disk means
to rotating means.
7. An apparatus according to claim 6, characterized in that said
upper disk means is provided with a centrally disposed opening and
in that said connecting means includes an agitating shaft means
extending through the centrally disposed opening and attached to
the upper side of said lower disk means.
8. An apparatus according to claim 7, characterized in that said
agitating shaft means is attached to the upper side of said lower
disk means by way of an annular cylindrical boss, said boss being
integral with said lower disk means.
9. An apparatus according to claim 6, characterized in that said
upper disk means is substantially smooth over the entire surface of
the upper side thereof up to the edges of said opening, said
opening being formed as a bore through said upper disk means, the
edges of said bore intersecting with the surface of the upper side
of said upper disk means such that said bore is open to the
surrounding medium in all directions above said upper disk
means.
10. An apparatus according to claim 6, characterized in that both
said flat blade means and said curved blade means extend
substantially perpendicularly with respect to the surfaces of the
respective disk means.
11. An aeration-agitating apparatus comprising a plurality of
radially extending flat blade means attached to the underside of a
lower circular disk means, a plurality of substantially radially
extending curved blade means attached at their bottoms to the upper
side of said lower disk means, an upper circular disk means
attached at the bottom side thereof to the tops of said curved
blade means, and connecting means for connecting at least one of
said disk means to rotating means, said upper disk means being
provided with a centrally disposed circular opening, each of said
curved blade means tapering downwardly from the edge of said upper
disk means which delimits the opening to respective points located
on the lower disk means radially inwardly from said edge.
12. An apparatus according to claim 1, characterized in that said
opening is formed as a bore through said upper disk means, the
edges of said bore intersecting with the flat upper surface of said
upper disk means such that said bore is open to the surrounding
medium in all directions above said upper disk means.
Description
The present invention relates to an improved agitating apparatus
for promoting gas-liquid contact reaction. More particularly, the
present invention is directed to an improved aeration-agitating
apparatus comprising disk means provided with a plurality of plate
means which cooperate to promote a gas-liquid contact reaction.
A gas-liquid reaction apparatus wherein gas is blown into a liquid
phase, or an apparatus used for the submerged culturing of aerobic
microorganisms, such as an agitating blade assembly, a turbine
having 4 to 6 flat blades, a turbine having curved blades, a disk
turbine having bottom blades, and the like, is well known. In these
type of apparatus, a gas is blown from the bottom side of said
apparatus by means of nozzles or a sparger and the gas bubbles
produced thereby are made finer and dispersed by a blade assembly.
However, it has been found that these flat blade or curved blade
turbines possess many disadvantages including a very large power
consumption which is necessary for obtaining a thorough contact of
the gas-liquid phase and for obtaining a high rate of gas
dissolution.
Although the disk turbine having bottom blades can give a large
shearing force to the gas-liquid mixture, and although a high rate
of gas dissolution can be obtained with a relatively low power
consumption, only a small amount of liquid is discharged by the
blade assembly and thus uniform agitation cannot be obtained in the
tank. Accordingly, the resulting insufficient mixing makes the
yield of reaction product lower.
Generally, an agitating blade assembly for an aeration agitating
tank must obtain a high rate of gas dissolution with a
corresponding low power consumption and a shortened mixing time
while obtaining uniformity or evenness throughout the entire tank.
Accordingly, it is desired to provide a blade assembly which will
give a high shearing effect to gas bubbles while utilizing as small
a power consumption as possible, thereby making said bubbles finer
and dispersing them uniformly throughout the entire reaction vessel
in a short period of time. Advantageously, the blade assembly
should discharge as much as is necessary to establish uniformity
throughout the entire reaction vessel and improve the circulating
flow in said vessel.
An object of the present invention is to avoid the prior art
disadvantages in the agitation of gas-liquid mixtures.
Another object of the present invention is to provide an improved
agitating apparatus for promoting gas-liquid contact reactions.
A further object of the present invention is to provide an improved
agitating apparatus which utilizes a low power consumption,
exhibits uniform agitation in a shorter mixing time and produces an
improved yield of reaction product.
A still further object of the present invention is to provide an
improved agitating apparatus which gives a high shearing effect to
gas bubbles thereby making said bubbles finer and disperses said
bubbles uniformly throughout the entire reaction mixture.
Other objects and further scope of applicability of the present
invention will become apparent from the detailed description given
hereinafter; it should be understood, however, that the detailed
description and specific examples, while indicating preferred
embodiments of the invention, are given by way of illustration
only, since various changes and modification within the spirit and
scope of the invention will become apparent to those skilled in the
art from this detailed description.
Pursuant to the present invention, it has been found that the
above-mentioned disadvantages may be eliminated and a much improved
agitating apparatus for promoting gas-liquid contact reactions may
be obtained by providing a blade assembly for the agitating
apparatus that gives a high shearing effect to gas bubbles with as
little a power consumption as possible, and by utilizing said
shearing effect to make finer gas bubbles and disperse said bubbles
uniformly throughout the entire reaction mixture.
The present invention will become more fully understood from the
detailed description give hereinbelow and the accompanying drawings
which are given by way of illustration only and thus are not
limitative of the present invention and wherein,
FIG. 1 is a perspective view of the agitating apparatus of the
present invention;
FIG. 2 is a side view of the agitating blade assembly of the
present invention;
FIG. 3 is a top view of the disposition of the curved plates
disposed between the upper and lower disk means; and
FIG. 4 is a bottom view of the disposition of the blade plates
attached to the bottom of the lower disk means.
Referring now to the drawings wherein like reference numerals are
used throughout the various views to designate like parts, the
apparatus of the present invention comprises a flat disk 1 provided
with a top cover 2, said elements being spaced apart by a plurality
of radially extending curved plates 3. The disk means 1 also
contains a plurality of radially extending blade plates 4 attached
to its bottom side. An agitating shaft 6 extends through an opening
in the top cover 2 and is attached to the top side of the flat disk
1 by means of a boss 7.
The flat plates 1 and blade plates 4 are usually called a disk
turbine having bottom blades, and are generally used in aeration
agitating tanks. A high rate of gas dissolution can be obtained
with a small unit power requirement by utilizing the blade assembly
according to the present invention. By providing curved blades 3, a
large discharging amount can be achieved with very little power
consumption, and the mixing time can be shortened. By rotating said
agitating blade assembly for aeration agitation, the liquid above
the agitating blade assembly is drawn in through a clearance
between the top cover 2 and the rotating shaft 6 and discharged by
the curved blades 3. Bubbles produced by a gas discharged from
nozzles or a sparger provided below the agitating blade assembly
are made finer and dispersed by the blade plates 4 and mixed with
the liquid discharged by the curved plates 3, and distributed
uniformly throughout the entire reaction mixture, whereby the
entire reaction mixture of the reaction vessel can be controlled to
a uniform dissolved gas concentration.
The blade plates 4 as referred to herein can be flat plates,
corrugated plates, curved plates, or the like, depending upon the
property of the liquid being agitated.
An agitating blade assembly using flat blade plates 4, as shown in
FIGS. 1, 2, 3 and 4, was employed in a 4-kl tank having a diameter
of 1,400 mm. The mixing time and the measured values of power
consumed are shown in Tables 1 and 2 at 200 and 300 r.p.m.,
respectively.
TABLE 1
Mixing time
Number of revolution 200 r.p.m. 300 r.p.m. Identification of blade
assembly
__________________________________________________________________________
Agitating blade assembly for aeration agitation of the 20 sec. 14
sec. present invention Turbine with 6 flat blades 29 sec. 21 sec.
Turbine with bottom blades 34 sec. 25 sec.
__________________________________________________________________________
TABLE 2
Consumed power
Number of revolution 200 r.p.m. 300 r.p.m. Identification of blade
assembly
__________________________________________________________________________
Agitating blade assembly for aeration agitation of the 5.1 H.P.
17.0 H.P. present invention Turbine with 6 flat blades 7.1 H.P.
24.4 H.P. Turbine with bottom blades 3.9 H.P. 13.0 H.P.
__________________________________________________________________________
table 1 shows the situation where 2.3 kl of water was charged into
a tank. 900 l per minute of air was introduced into the water and
agitation was conducted at 200 r.p.m. and 300 r.p.m., respectively.
A pH meter of the immersion type was placed in the tank and while a
caustic soda solution was added to the top of said tank, the time
required for the pH to become constant was measured. As can be
readily noted, the mixing time for the same number of revolutions
is shorter when using the agitating blade assembly of the present
invention when compared to the flat blade turbines and the
bottom-blade disk turbines of the prior art. Table 2 shows the
power required for agitation when 900 l per minute of air was
introduced into the tank and measured by a strain gage.
According to Tables 1 and 2, a mixing time of 20 seconds can be
obtained with 5.1 H.P. when using the agitating main assembly of
the present invention, whereas when using a flat blade turbine and
a bottom-blade disk turbine, mixing times could not be reduced to
20 seconds, even when using 24 H.P. and 13 H.P., respectively.
Table 3 shows the results of a measurement of the sodium sulfite
oxidation rate obtained by operations similar to that shown in
Tables 1 and 2.
TABLE 3
Sodium sulfite oxidation rate (Kg-mol/m.sup.3.hr.atm.)
Number of revolution 200 r.p.m. 300 r.p.m. Identification of blade
assembly
__________________________________________________________________________
Agitating blade assembly for aeration agitation of 0.600 1.238 the
present invention Turbine with 6 flat blades 0.333 1.143 Turbine
with bottom blades 0.381 0.570
__________________________________________________________________________
The sodium sulfite oxidation rate is lower but power consumption is
higher when using the flat blade turbine rather than the agitating
blade assembly of the present invention, when compared at the
respective r.p.m. For example, only 0.570 kg-mol/m.sup.3 hr.atm. is
obtained with a power consumption of 13.0 H.P. in the case of the
bottom-blade disk turbine, and thus the power efficiency is not as
good as the agitating blade assembly of the present invention.
The invention being thus described, it will be obvious that the
same may be varied in many ways. Such variations are not to be
regarded as a departure from the spirit and scope of the invention,
and all such modifications as would be apparent to one skilled in
the art are intended to be included within the scope of the
following claims.
* * * * *