JP2004283796A - Aeration system for liquid required to be activated - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide an aeration system constituted in such a manner that a liquid required to be activated in a storage tank for the liquid required to be activated of a large sink or in rivers, lakes, ponds, or the like, is circulated and flowed by being accompanied by a chimney effect and is mixed and stirred in a uniform manner when aeration is performed by sinking a static mixer in a vertical form into the liquid required to be activated. <P>SOLUTION: When the square mixer 1b is sunk into the storage tank for the liquid 11 required to be activated and air is sent and circulated together with the liquid 11 required to be activated therein to treat the liquid, circulation is generated and the air is dispersed and made finer during the flow such that the liquid is uniformly dispersed, mixed and stirred, a uniform concentration of dissolved oxygen is obtained and effective aeration is performed. According to this system, the circulation, mixing and stirring in the storage tank for the liquid required to be activated are performed simultaneously with the aeration without the occurrence of clogging, and the like, in a nozzle during the aeration when the aeration takes place in the storage tank for the liquid required to be activated. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

[0001]
[Industrial applications]
The disclosed technology performs aeration through a scale mixer for an activated liquid required to increase dissolved oxygen in an activated sludge storage tank, river, lake, etc., and circulates with a chimney effect. The system belongs to the technical field of a system that performs uniform dispersion, mixing, and stirring.
[0002]
[Prior art]
As is well known, recently, the amount of dissolved oxygen such as contaminated waste liquid is increased, the required amount of the activating liquid is stored in a predetermined activating liquid storage tank, and the circulating liquid is circulated through a sedimentation of a static mixer or the like. In the passing process, various types of aeration systems for performing aeration have been put to practical use in the chemical industry and the like, and the aeration systems described in the following patent documents and the like have been put to practical use.
[Patent Document 1]
JP 2000-334485 A
[Patent Document 2]
JP-A-11-90197
[Patent Document 3]
JP-A-2002-273468
[Patent Document 4]
JP 08-117787 A
[Patent Document 5]
JP 09-47777 A
[Patent Document 6]
JP-A-54-18473
[Patent Document 7]
JP-A-55-8835
[Patent Document 8]
JP-A-56-129092
[Patent Document 9]
JP-A-56-166992
[Patent Document 10]
JP-A-58-14996
[Patent Document 11]
JP-A-01-99693
[0003]
[Problems to be solved by the invention]
Incidentally, in the aeration system of the type described above, in the process in which the aeration device simply deposits a pipe mixer such as a static mixer in the activating liquid storage tank and forcibly circulates the activating liquid. In order to provide a simple system for performing aeration in the static mixer, first, the pipe mixer of the static mixer of the aeration apparatus basically requires mixing and stirring between the activating liquid and the air. This is only performed during the flow of the activating liquid, and therefore, when the air nozzle for aeration provided in the air supply pipe is in the form of fine bubbles, there is a drawback that clogging occurs with the activating liquid. Therefore, the efficiency of the nozzle is reduced during operation, and maintenance and maintenance for the clogging of the nozzle must be performed each time. Becomes worse, there is inconvenience that aeration as designed is not performed, also the distribution of dissolved oxygen is biased to its site shade, uniform distribution there is a disadvantage not observed.
[0004]
[Object of the invention]
An object of the invention of this application is to provide an aeration device such as a pipe mixer based on the above-mentioned conventional technology in an activated sludge storage tank, a river, a lake, a marsh, or the like, in which an oxygen-deficient state or a putrefactive state requiring a large amount of dissolved oxygen. Deposits in a vertical state, etc., in order to solve the problem of poor operation efficiency of aeration, etc., and turns with respect to the deposited line mixer of the scale mixer to be stored in the activating liquid. In the process of circulating flow, squeezing and enlarging are repeated as much as possible with a chimney effect to disperse, dispersing and distributing the dissolved oxygen to a uniform state, and ensuring the predetermined mixing and stirring, and Promotes the miniaturization of air bubbles and ensures that aeration as designed is performed with a chimney effect during aeration, regardless of the size of the air nozzle, to achieve aeration technology applications in the chemical equipment technology industry. Benefit Is to St. provide aeration system for superior main activating liquid.
[0005]
【means】
In order to solve the above-mentioned problems, a configuration of the invention of the present application for solving the above-mentioned problem in an aeration system for an activation-requiring liquid in accordance with the above-mentioned object is to provide an axial center of a pipe in the activation-requiring liquid. A plurality of blades having a center corresponding to each other intersect with each other, and a pipe mixer of a scale mixer is vertically deposited in the activating liquid to be disposed below the pipe mixer of the scale mixer. The air and the activating liquid are circulated upward with a chimney effect so that the activating liquid flows through the pipe, and the activating liquid flows into the pipe mixer while being circulated. The main requirement is to mix and disperse air to perform aeration of the activating liquid, so that the activating liquid may have a large activity required by the sink during the circulation of the activating liquid. So that it can be dispersed, mixed and stirred in the liquid storage tank. The supply of air to the pipe mixer is performed by a large-diameter nozzle, and a plate or a rod-like projection that promotes dispersive mixing in either the unit element of the above-mentioned scale mixer and / or the pipe, or both. A jig having pieces is provided, and a scale mixer having the shape of claim 4 is used as a mixing and dispersing device for gas, liquid, powder, or a combination thereof. In addition, technical measures are taken such that the above-mentioned activating liquid is an activating liquid required for rivers and lakes.
[0006]
[Action]
In the above-described configuration, a large amount of the activating liquid, such as a large activating liquid storage tank of a sink, a river, a lake, or the like, is subjected to aeration in the activating liquid containing a predetermined amount of the activating liquid, and halfway through the process. When aeration is performed, the flow is performed such that the center of the blade is present so that the center of the pipe mixer of the scale mixer deposited vertically in the activation liquid is required. At this time, the air that is supplied causes a chimney effect to cause a swirling flow from the bottom to the top of the pipe mixer, uniformly dispersing and diffusing, promoting the miniaturization of bubbles, and aeration along with the chimney effect along the way. In addition, even if the air bubbles are fine, the miniaturization is promoted and clogging does not occur, no maintenance and inspection is required, and the average dispersion, mixing and stirring are performed by repeating squeezing and expansion, In addition, it is designed to promote the miniaturization of bubbles. A jig having projections for promoting the activation is further provided in the flow path of the activating liquid, so that the concentration of the dissolved oxygen can be averaged and uniform. To promote the activation.
[0007]
Also, in the process where the activating liquid flows through the pipe mixer of the scale mixer by the lift action together with the air, the division and the current change by the blades in the scale mixer are repeatedly performed, and the squeezing and expansion are performed. Is repeated, a chimney effect is generated, and swirling, dispersion, mixing, and stirring are reliably performed, miniaturization of air bubbles is promoted, and activation of the activating liquid is effectively performed. It is.
[0008]
DESCRIPTION OF THE PREFERRED EMBODIMENTS
Next, a mode in which the invention of the present application is to be implemented will be described as an embodiment with reference to FIGS.
[0009]
First, a static mixer pipe mixer 1 as shown in FIG. 8 called a so-called line mixer is devised by Kenix, and an element 4 in which one unit blade 3 is twisted by 90 degrees in a pipe 2 of the pipe. , 4,... Are abutted and connected to each other with a phase shift of 90 degrees to each other, and a desired number of a plurality of them are arranged in the axial direction. A variety of techniques have been developed in which the division and rotation of the activating liquid is repeated to achieve dispersion and mixing and stirring.
[0010]
However, in the static mixer 1 of the pre-developed line mixer, one unit element 4 of the unit blade 3 provided in the pipe 2 having a circular cross section is twisted by 90 degrees. In the case of the small-size line mixer 1, the molding process is easy, but in the case of the large-size static mixer line mixer 1, the forming process of the element 4 is extremely difficult. However, there is an inconvenience that the cost is increased.
[0011]
In order to cope with this, as shown in a scale mixer 1a of the invention of the applicant's earlier application as shown in FIG. An element in which flat plate-like isosceles triangular unit blades 3a, 3a are opposed to each other, and other isosceles triangular unit blades 6, 6 are erected on the intersecting sides 5, 5 to be integrally extended. A pipeline mixer 1a having a 4a was developed (trade name: scale mixer), and the division and transformation of the activating liquid flowing in the feed flow were geometrically repeated to perform pinching and release, and a vertical type. In the state in which the mixer is arranged in a state, a chimney effect is generated during the use of the lift, so that extremely efficient mixing and stirring can be performed, and a technique for promoting the miniaturization of bubbles has been developed. Based on pipe mixer 1a Various pipeline mixer have been developed by.
[0012]
However, when manufacturing a large-sized pipe mixer 1a, it is difficult to obtain a pipe 2a having a rectangular cross section, and it must be specially ordered. There was a disadvantage of becoming.
[0013]
In order to cope with this, for example, a scale mixer 1b as shown in FIG. 2 of the applicant's new invention disclosed in Japanese Patent Application Laid-Open No. 7-63597 has been developed. Have been improved.
[0014]
【Example】
In the embodiment shown in FIG. 1, reference numeral 1d denotes a liquid storage tank for storing a large amount of the activating liquid 111 having a large sink in a set amount, and a scale mixer 1b is vertically deposited near the bottom thereof. It is so. In the invention of this application, the activating liquid 111 may be not only the storage tank 1d having a large sink, but also an activating liquid in an oxygen-deficient state or a putrid state such as a river or a lake.
[0015]
Reference numeral 1b denotes a pipe mixer of a scale mixer which forms the center of the gist of the invention of this application, and its pipe 2a is a circular pipe of a predetermined size or a commercially available pipe (a square pipe may be used depending on the design). The cylindrical tube 2a shown in FIG. 2 has a pair of isosceles triangular plate-shaped blades 3b, 3b having the same axis as the axis, and their vertexes are opposed to each other in common. The other pair of flat plate-shaped blades 6a, 6a each having an arc-shaped peripheral portion intersecting each other at a predetermined angle on each of the oblique sides intersecting each other are provided so as to be in the same plane. The blades 3b extend in opposite directions at right angles to the blades 3b.
[0016]
An air supply pipe 2b has a large diameter air nozzle of a predetermined size facing the scale mixer 1b at the lower part of the scale mixer 1b.
[0017]
In the aspect in which the scale mixer 1b is deposited and disposed in a vertical state, the activating liquid 111 flowing through the blades 3b and 6a is twisted and swirled by air to urge the lift-up action during the flow. In particular, when it is arranged in a vertical state, a so-called chimney effect is exerted due to the lift action, and in the process, the miniaturization of bubbles is promoted.
[0018]
The other pair of flat blades 6a, 6a intersect with the pair of blades 3b, 3b as horizontal split plates while being flat, and all edges of the pair of blades 6a, 6b are of the tubular body 2a. As described above, the pair of flat blades 6a, 6a, which come into contact with the inner wall and flow the fluid flowing from one side of the circular tube 2a, function as a current changing plate, and convert the flowing fluid to the back side. It is made to shed.
[0019]
The scale mixer 1b is vertically deposited on the bottom of the activating liquid 111. The activating liquid 111 is squeezed, released, circulated and lifted in the storage tank 1d. In this case, the chimney effect works sufficiently, the aeration effect is promoted by accelerating the miniaturization of bubbles from the air nozzle 2b, and the effect during circulation of the activating liquid can be added to the chimney effect. By positively applying the air jet from the air nozzle 2b to the scale mixer 1b, the chimney effect and the miniaturization of bubbles cause aeration of the activating liquid in the lift.
[0020]
In the unit element 4a thus configured, one isosceles triangular blades 3b, 3b opposed to each other in a circular pipe 2a circumscribing in the axial direction are formed in opposed portions on one side opposed to each other. As shown in FIG. 2, through the slits 7 (instead of the slits 7, they can be integrally joined by welding), they are brought into contact with each other in a meshing state, and the front and rear unit elements 4 a, 4 a are circumferentially opposed by the slits 7. Are prevented from rotating, so that the unit elements 4a, 4a,... Connected adjacently in the axial direction are not only connected in the axial direction but also connected to each other in a non-rotating manner in the circumferential direction. become.
[0021]
As shown in FIG. 3, since each unit element 4a is provided with a phase shift of 90 degrees in the circumferential direction in the arrangement connected in the axial direction, the blade of one flat plate-like unit element 4a is provided. 3b functions as a dividing plate as described above, and the other pair of flat blades 6a, 6a function as current changing plates, so that the unit element 4a increases the flowing fluid stepwise in the axial direction. By doing so, the number of divisions is increased by a geometric series times two, forming an average variance and adding a current change to promote extremely high dimensional division and subdivision. Mixing and agitation are performed while repeating the release, the chimney effect, and the generation of the swirling flow. In addition, no turbulent flow occurs in the circular pipe 2a, and therefore, the pressure loss and the energy loss are small, and the activation liquid is required. 1 Energy required for mixing and stirring by utilizing the first stream is also one in which fewer.
[0022]
In the aspect in which the activation liquid 111 is vertically deposited from the scale mixer 1 in the activation liquid 111, a lift effect is generated while the activation liquid 111 is flowing out, and a chimney effect of forcibly raising the flow is generated. At the same time, the circulation of the activating liquid 111 is performed.
[0023]
The activating liquid 111 flowing through the unit elements 4a tends to receive a circumferential turning reaction force by the flow changing function of the other multi-stage flat blades 6a, 6a. As shown in FIG. 5, at one of the multi-stage unit elements 4a, 4a, for example, at the beginning or end, the ring 8 is spot-welded 9 to form one plate-like split plate of the unit element 4a. The unit element 4a is integrally fixed to the end of the blade 3b and fastened together with the end flange 10 of each of the unit circular tubes 2a, 2a, so that the unit element 4a is integrally fixed to the circular tube 2a and has a circumferential turning reaction force. , And the unit elements 4a are engaged with each other through the slits 7 as shown in FIG. 5, so that all the elements 4a, 4a... It will not be coordinated.
[0024]
Thus, as shown in FIG. 5, the connection and connection of the unit elements 4a, 4a in each stage are performed by engagement with the slits 7, but as in the embodiment shown in FIG. It is also possible to form slits 7, 7, which are formed so as to face each other and have a phase difference of 90 ° opposite to each other, as blades 4 b, 3 b as a dividing plate of 4 a, so that the mutual slits 7, 7 mesh with each other. good.
[0025]
Instead of the slits 7, they can be connected to each other in a fixed state by welding.
[0026]
In the embodiment shown in FIG. 7, a blade serving as one of the divided plates of the unit element 4a is provided as an anti-rotation for one unit element 4a by a suitable stopper 11, 11 near the flange 10 of the cylindrical tube 2a. 3b, and a stopper (not shown) is formed inside the vicinity of the flange 10 of the circular tube 2a as shown in FIG. It is also possible to use a detent for 4a.
[0027]
In the above-described configuration, the unit elements 4a, 4a,... Are formed inside the circular tube 2a via the slits 7 formed in the blade 3b of one of the flat plate-like divided plates of the adjacent unit elements 4a, 4a. As described above, it is also possible to abut and engage in combination with each other and to continuously insert and set a predetermined number of stages in the circular tube 2a in the axial direction in a multi-stage arrangement. In the unit element 4a, the other flat blade 6a, which extends 90 degrees crosswise to one flat split plate blade 3b and extends outward, has its entire outer peripheral edge portion in contact with the inner wall of the circular tube 2a. The fluid is prevented from leaking from the blade 6a in the circumferential direction.
[0028]
When the activated sludge 111 of the activating liquid is fed from one side of the circular tube 2a in the state set as described above, the activating liquid 111 is divided into two by one flat blade 3b, and immediately The current is changed to the opposite side by the other flat blades 6a, 6a, then to the next unit element 4a, and further divided into two by the split plate of the blade 3b of the one flat plate unit element 4a. Squeezed, and then transformed in the opposite direction by the blades 6a of the current-distribution plate, are geometrically divided, transformed, swirled, and the concentration of high dissolved oxygen is made uniform and uniform. Dispersion is repeated with a chimney effect, during which a vigorous stirring action results in a uniform dispersion in the circumferential direction, and in the axial direction astronomical splitting, transformation, dispersion, mixing and stirring. Through Pinched and distributed swivel been conducted by stirring a mixed is performed on the main activating solution 111, also circulating swirl flow 2c can be smoothly.
[0029]
During this time, circumferential reaction forces are applied to the unit elements 4a by the blades 6a of the current change plate in the flow-through process of the activating liquid 111 in the tube 2a. , 4a are connected by a slit 7 and one unit element 4a does not rotate in the circumferential direction because one unit element 4a is subjected to the circumferential detent action by the flange 10, so that each unit element 4a is located inside the circular pipe 2a. Can maintain a fixed posture.
[0030]
During this time, predetermined air is supplied from an air nozzle 2b of 4φ or the like, and is blown out from a large-diameter nozzle 2b of a large diameter at its tip, for example, to a predetermined aeration action on the activating liquid 111. The aeration 112 is performed, and the rise of bubbles is further promoted by the chimney effect, a circulating swirl flow is also generated, and aeration is also promoted, and a predetermined action is performed on the activating liquid 111. Unnecessary maintenance is performed without clogging of 2b.
[0031]
During this time, even if the air nozzle 2b is on the side of the activating liquid 111, clogging does not occur and aeration is smoothly maintained even in the state of fine bubbles.
[0032]
Then, during the circulation of the activating liquid 111, the high concentration of dissolved oxygen is dispersed throughout the deep storage tank and large volume by repeating the squeezing, releasing, chimney effect, and circulating effects, and the concentration is uniform. Is held.
[0033]
Thus, at the time of initial production and assembly, the pipe is easy to obtain because the pipe is the circular pipe 2a, and it is hardly necessary to perform molding or the like, and each of the elements 4a is made of a flat plate made of the blades 3b and 6a. Therefore, the molding process is extremely easy and can be performed at low cost.
[0034]
When the tube 2a having a unit length is connected to a predetermined length through the flange 10, one of the plate-like blades 6a of the unit element 4a is connected to the unit 2 at the flange 10 by 90 degrees. If the phase is changed in the circumferential direction and fixed, the unit elements 4a, 4a,... Arranged in a large number in the axial direction over the entire length of the tubular body 2a of the design length are provided as those having different phases in the circumferential direction. In addition, any of the unit elements 4a is prevented from rotating in the circumferential direction.
[0035]
It should be noted that the embodiments of the invention of this application are not limited to the above-described embodiments. For example, the inner surface of the tube 2a and the blades 3b and 6a may be processed with Teflon (registered trademark), or the unit element may be used. Various modes such as providing a bulkhead at a predetermined portion of the present invention can be adopted. Further, in the design mode, the bridge type (in the scale mixer 1b, the dividing plate and the current changing plate are not connected to each other continuously as in the embodiment of FIG. 1 but are partially omitted in the axial direction). There is also a mode in which the activating liquid 111 enters from the missing portion to assist circulation.) The target activating liquid is not only the liquid to be stored in the storage tank 1d, but also the activating liquid such as a drainage liquid or a slurry requiring a predetermined amount of decaying or oxygen-deficient or dissolved oxygen in a river or a lake. Is also targeted.
[0036]
Further, in the case of the scale mixer 1b, the upper, lower or middle of the unit 4 and the baffles 8, 8,..., The mesh plate as shown in FIGS. It is possible to arrange a jig which is more likely to activate the stirring rods 9, 9 ..., bulkheads and the like than those which easily cause scattering, and the jigs 8, 9 have a plate-like cross section. Various shapes such as a polygonal shape, a round shape and a rod shape can be adopted, and can be integrally implanted in the unit blades 3a and 6b, the tube 2a and the like.
[0037]
Further, the jigs 8 and 9 promote the miniaturization of bubbles during aeration, and the resistance of the aeration is negligible.
[0038]
Further, the inflow portion of the slurry requiring activation liquid 111 can be disposed at a portion between the units 4 and 4.
[0039]
The tube 2a and each of the blades 3b and 6a can be left to an appropriate design change without specifying the material of the metal or the resin product.
[0040]
After completion of the mixing of the conduit with the predetermined activation liquid 111, various cleaning fluids are caused to flow through the pipe, so that the cleaning fluid again performs geometrical mixing and stirring in the flowing process. Therefore, complete cleaning can be performed, and mixing and stirring of impurities does not occur in the next mixing and stirring.
[0041]
In the invention of this application, the activating liquid not only increases the amount of dissolved oxygen, but the liquid in a state of oxygen deficiency or decay such as a river or a lake is also used for a slurry in a chemical factory or the like. Generally applicable.
【The invention's effect】
As described above, according to the invention of this application, without using any unit driving devices such as a mixer or a stirrer, a uniform mixer is used by a scale mixer in a process of flowing an activating liquid into a pipeline. Dispersion is performed, and the mixing and stirring are automatically performed geometrically in order. The basic merits of the line mixer of the static mixer are fully utilized, and the dispersion and mixing as designed are promoted. Each unit element does not rotate in the circumferential direction and is prevented from rotating even when the current is changed, so that the rigidity and strength of the entire device are maintained, there is no backlash, good durability, and movable parts Because of the absence of the above, there is no need to perform maintenance such as maintenance and inspection, and there is an effect that the life of the pipe mixer is long.
[0042]
And even if the air nozzle for aeration has a large diameter, regardless of the size of the air bubbles during aeration, and even if the miniaturization of air bubbles is promoted, the squeezing and release of the activating liquid and the chimney effect can be achieved. An excellent effect is achieved in that the aeration is effectively performed by repeated mixing and stirring.
[0043]
In addition, since the aeration in the lift process using the large-diameter nozzle is performed more reliably, an excellent effect is obtained in which the effects of raising, mixing, and stirring the activating liquid are obtained.
[0044]
Since the scale mixer has no moving parts, there is no vibration or noise during operation, and the working environment is kept quiet.
[0045]
Thus, with respect to a predetermined number of a plurality of multi-stage unit elements arranged in multiple stages in the axial direction, the other flat plate blade forming the current transformer crosses the flat blade forming the dividing plate. As a result, the power is divided by a power of 2 for the number of unit elements arranged, and the flow is changed so that uniform dispersion and mixing can be efficiently performed while squeezing and releasing. This has the effect.
[0046]
And, in the process of diffusion division and transformation in the activation liquid storage tank or the like, since the stirring is performed in the whole area, the activation liquid in the flowing circulation is uniformly dispersed and diffused, and the squeezing and releasing are performed. The activating liquid is uniformly stirred and mixed, and sedimentation and sedimentation of solids in the activating liquid are prevented, not only clogging of the air nozzle is prevented, but also the concentration of the activating liquid is kept constant, An excellent effect that aeration is maintained is achieved.
[0047]
Further, since all the peripheral portions of the blades as the other flat current-distribution plates are in contact with the inner surface of the circular tube, no leakage occurs in the other blades, and the current is reliably changed. As a result, there is an advantage that uniform dispersion, mixing and stirring can be efficiently performed, and physical and chemical effects are maintained.
[0048]
And since the tubular body uses a circular pipe, it is easier to obtain than a square tubular body, etc., and it is possible to reduce the cost because there is no need to manufacture a special tubular body. It has the advantage of being particularly effective when made.
[0049]
Also, since all the internal unit elements are manufactured with a flat plate, they can be assembled only by cutting or welding, there is no bending, etc., so the number of steps is small, assembly is easy, and the initial assembly and set state is driven. There is also an effect that it can be maintained even inside.
[0050]
Further, since the unit element is provided with a plate or a jig having a bar-shaped protruding piece, an excellent effect of promoting aeration is provided.
[0051]
And even in a large activation liquid storage tank having a large sink, a single scale mixer is deposited vertically in the activation liquid and aerated, so that even if the scale mixer is small in size, Even if the amount of the activated sludge scale mixer is large, an excellent effect that aeration can be performed is exhibited.
[Brief description of the drawings]
FIG. 1 is an overall schematic perspective view of an embodiment of the present invention.
FIG. 2 is a perspective view of an element of a scale mixer.
FIG. 3 is a perspective view in which the unit element is prevented from rotating around a tube.
FIG. 4 is an enlarged perspective view of a connection portion between the unit elements.
FIG. 5 is an enlarged perspective view of another embodiment corresponding to FIG. 4;
FIG. 6 is a perspective view of a unit element and a pipe of another embodiment, which are not rotated.
FIG. 7 is a perspective view corresponding to FIG. 6 of still another embodiment.
FIG. 8 is a perspective view of a static mixer according to the prior art.
FIG. 9 is a partially transparent enlarged perspective view of a pipe mixer of a scale mixer according to the invention of the prior application.
FIG. 10 is a partial perspective view of another embodiment of the present invention.
FIG. 11 is a partial perspective view of still another invention of this application.
FIG. 12 is a perspective view of another embodiment.
[Explanation of symbols]
1a Pipeline mixer
1d storage tank
111 Activation liquid required
1b Scale mixer
2a, tube, circular tube
3b, 6a blade
2b Aeration nozzle, air supply pipe
112 Aeration
4a Unit element
7 slit
8 Baffles
9 stir bar
10 Flange
11, 12 stopper
2c Circulating swirling flow
8,9 Jig with projections to further activate the sulfur activating liquid

Claims (6)

In the aeration system for an activating liquid, a line mixer of a scale mixer in which a plurality of blades having a center coinciding with the axis of a pipe in the activating liquid intersect with each other is provided. The activating liquid is deposited in a vertical state in the liquid, and the air and the activating liquid are circulated from the lower part of the pipe mixer of the scale mixer to the upper part in accordance with the chimney effect. Aeration of the activating liquid required by mixing and dispersing air in the circulating fluid of the activating liquid with respect to the pipeline mixer to perform aeration of the activating liquid. system. 2. The method according to claim 1, wherein the activating liquid is dispersed, mixed and stirred in the activating liquid storage tank having a large sink during the circulation of the activating liquid. Aeration system for activating liquid. 3. The aeration system for an activating liquid according to claim 1, wherein the supply of air to the conduit mixer is performed by a large-diameter nozzle. Activation required for a unit element of the above-mentioned mixer mixer and / or a pipe or a jig having a rod-like projection piece disposed thereon for promoting dispersion mixing. Aeration system for liquids. An aeration system for an activation-requiring liquid, wherein the scale mixer having the shape of the above-mentioned claim 4 is used as a device for mixing and dispersing gases, liquids, powders, or a combination thereof. 2. The aeration system for an activation-requiring liquid according to claim 1, wherein the activation-requiring liquid is an activation-requiring liquid for a river or a lake.

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