JP2516172B2 - Gas-liquid mixing device - Google Patents

Description

Detailed Description of the Invention

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gas-liquid mixing apparatus for dissolving and dispersing a gas in a liquid under high pressure to produce a liquid which generates a large number of fine bubbles at a low pressure.

[0002]

2. Description of the Related Art The conventional gas-liquid mixing device is shown in FIG. 1 shown in FIG. 7 is a high-lift centrifugal pump,
Reference numeral 2 is a compressor, 3 is a pressure tank, and 4 is a pressure reducing valve. The centrifugal pump 1 is rotationally driven by a motor (not shown), sucks water from the suction port 5 under atmospheric pressure, and discharges high-pressure water from the discharge port 6. This high-pressure water flows into the pressure tank 3 through the communication pipe 7. On the other hand, the compressor 2 sucks air from the suction port 8,
The sucked air is compressed and supplied into the pressure tank 3 through the communication pipe 9. As a result, the pressure inside the pressure tank 3 becomes high, and the air 11 is dissolved in the water 10. Further, since the compressed air 11 is blown into the pressure water 10 in the pressure tank 3, the compressed air 11 can be dispersed in the pressure water 10. Next, when the water in which a large amount of air is dissolved under high pressure is discharged from the pressure tank 3 and returned to the atmospheric pressure (low pressure) through the pressure reducing valve 4, a large amount of fine air is dissolved in the water. Appears as bubbles and rises toward the surface of the water. In this way, it is possible to produce water that generates a large amount of bubbles in water.

This gas-liquid mixing device is used, for example, in a floating separation system in a wastewater treatment process. The floating separation method is a method of mixing suspended water containing floating substances with poor sedimentation with water containing a large amount of bubbles, and attaching the bubbles to the floating substances when the bubbles float in the dirty water. This is a method in which the specific gravity of is reduced and the suspended solids with reduced specific gravity are floated on the surface of the sewage and separated.

However, in the conventional gas-liquid mixing apparatus shown in FIG. 7, the compressor 2 and the pressure tank 3 are required, so that the apparatus becomes bulky and the cost of the apparatus as a whole becomes high.

In order to solve the above problem, a gas-liquid mixing device shown in FIG. 8 has been devised. In FIG. 8, 12 is a high-lift centrifugal pump, and 13 is an injector. As shown in FIG. 6, the injector 13 includes a nozzle 14 and a blowout portion 15 that is screwed into the nozzle 14,
An air intake 16 is formed in the peripheral wall of the blowout portion 15. When water is supplied from the inlet 17 of the nozzle 14, the water is ejected from the outlet 20 through the nozzle hole 18 and the blowing hole 19. In addition, when the water passes through the room 21 formed at the inlet of the blowing unit 15, the air at the atmospheric pressure can be drawn in and taken in from the air intake port 16, whereby the water entrained in the air can be drawn into the blowing unit 1.
5 can be ejected from the outlet 20.

According to this gas-liquid mixing device, when the centrifugal pump 12 is driven, water passes through the suction pipe 22 and is branched into two at the outlet of the suction pipe 22, one of which passes through the communication pipe 23 and the centrifugal pump 12 is driven. 12 flows into the suction port 24, and the other flows into the suction port 24 through the communication pipe 25 in which the injector 13 is provided. Therefore, the pump 12
Water mixed with air flows in, and the pump 12 can stir the water mixed with air by the rotation of an impeller (impeller) to dissolve and disperse the air in the water. The pressure in the pump 12 is increased by the rotation of the impeller. Then, the water in which this air is dissolved is discharged through the discharge port 26.
Discharge more. The water discharged from the discharge port 26 generates many bubbles under the atmospheric pressure.

[0007]

However, in the gas-liquid mixing device shown in FIG. 8, since the air is sent into the pump 12 together with the water, the ability of the pump 12 to push out the water is lowered (the impeller is idling). However, there is a problem that the water pressure cannot be raised to high pressure. As described above, when the pressure in the pump 12 is not high, that is, when the pressure is low, the amount of air that can be dissolved in water is small, and therefore the pump 1
There is a problem that the water discharged from the second discharge port 26 can generate only a small amount of bubbles under the atmospheric pressure. As a result, there is a problem that, for example, in the wastewater treatment process, the chances of air bubbles adhering to the floating substance are reduced, and the amount of the floating substance that can be floated on the surface of the wastewater is reduced.

An object of the present invention is to provide a gas-liquid mixing device which is small in volume, has a simple structure, and is inexpensive.

[0009]

The gas-liquid mixing device of the first invention has a first suction port for sucking the liquid, and a first discharge port for discharging the liquid sucked from the first suction port. A first pump and a first pump communicating with the first discharge port
Second inlet for sucking the boosted pressure liquid body by,
And a second pump having a second discharge port for discharging the liquid sucked from the second suction port, and the liquid discharged from the second discharge port provided at the second discharge port is decompressed and delivered. Pressure reducing device and the first port sucked into the second suction port.
And a gas inflow means for mixing gas in the pressure liquid pressurized by the pump .

The gas-liquid mixing device of the second invention comprises a first pump having a first suction port for sucking the liquid, and a first discharge port for discharging the liquid sucked from the first suction port, A second pump having a second suction port communicating with the first discharge port and a second discharge port discharging the liquid sucked from the second suction port; and a second pump provided at the second discharge port. Two
A pressure reducing device that reduces the pressure of the liquid discharged from the discharge port of the second discharge port, a communication pipe that connects the second discharge port and the second suction port, and a second discharge port provided in the middle of the communication pipe. And an injector capable of sucking gas from the outside of the communication pipe and entraining it in the liquid when the liquid flowing into the communication pipe from the inside passes through the inside.

[0011]

According to the first aspect of the invention, when the first pump and the second pump are driven, the first pump sucks the liquid from the first suction port and discharges the liquid from the first discharge port, The pump
The liquid discharged from the first discharge port is sucked from the second suction port and discharged from the second discharge port. The liquid ejected from the second ejection port is decompressed by the decompression device and delivered. Thereby, the pressure of the liquid in the flow path between the first ejection port and the second ejection port can be increased mainly by the first pump and the second pump. And the gas inflow means is the first pump sucked into the second suction port .
Can be made to flow into the gas body pressure liquid boosted me. This allows the gas to flow into the second pump. As a result, the second pump can stir the liquid mixed with the gas by the impeller under a predetermined high pressure, so that the gas can be dissolved and dispersed in the liquid.

In the second aspect of the invention, since the second discharge port and the second suction port of the second pump are communicated with each other by the communication pipe, a part of the liquid discharged from the second discharge port is It returns to the second suction port through the communication pipe and again passes through the second pump. Then, when the liquid passing through the inside of the communication pipe passes through the inside of the injector, the gas is sucked and entrained from the outside of the communication pipe, and the gas is mixed with the liquid. The liquid mixed with the gas merges with the liquid discharged from the first discharge port and flows into the second pump. In this way, the liquid mixed with the gas flowing into the second pump can be agitated by the impeller of the second pump under a predetermined high pressure, as in the first invention, and the gas is thereby mixed. It can be dissolved and dispersed in a liquid.

[0013]

DESCRIPTION OF THE PREFERRED EMBODIMENTS A first embodiment of the present invention will be described with reference to FIG. The gas-liquid mixing apparatus of this embodiment is used, for example, in a floating separation system in a wastewater treatment process. That is,
The gas-liquid mixing device shown in FIG. 1 sucks in water 28 containing no suspended solids (hereinafter, referred to as fresh water 28) stored in a tank 27, and dissolves and disperses air in the fresh water 28 under high pressure. Then, the fresh water in which the air is dissolved is decompressed and supplied into the sewage 29 containing suspended substances. Then, as described in the conventional example, when the air bubbles 30 float on the wastewater 29 and adhere to the floating substance, the specific gravity of the floating substance can be reduced, and the floating substance having the reduced specific gravity is transferred to the surface of the wastewater. To separate it.

Reference numeral 31 shown in FIG. 1 is a first pump, 32 is a second pump, 33 is a pressure reducing device, and 34 is a gas inflow means.

The first pump 31 is a centrifugal pump. However, the pump is not limited to the centrifugal pump, and other pumps can be used. In short, the first pump 3 has a function of giving energy to the sucked water.
It is sufficient that the pressure in the second pump 32 communicating with 1 can be raised to a predetermined pressure. Although not shown in the drawing, the first pump 31 is connected to a motor and is rotationally driven by this motor. Then, as shown in FIG. 1, the first suction port 35 of the first pump 31.
Is connected to one end of a suction pipe 36, and the suction pipe 3
The other end of 6 is immersed in fresh water 28. First pump 3
The first discharge port 37 of No. 1 and the second suction port 38 of the second pump 32 are in communication with each other via communication pipes 39, 40 and a T-shaped connection pipe 41.

The second pump 32 is a centrifugal pump. However, the pump is not limited to the centrifugal pump, and other pumps can be used. What is essential is that it has a function of giving energy to the sucked water and a function of stirring fresh water and air flowing inward. Although not shown in the figure, the second pump 3
Reference numeral 2 is connected to a motor and is rotationally driven by this motor. Then, as shown in FIG. 1, the second discharge port 42 of the second pump 32 communicates with the inlet of the decompression device 33 via the communication pipes 43, 44 and the T-shaped connection pipe 45.

The decompression device 33 is a decompression valve, and decompresses high-pressure fresh water in which the air flowing in from the inlet is dissolved to an atmospheric pressure and discharges it through the outlet and the discharge pipe 46.

The gas inflow means 34 is provided with the injector 13 as shown in FIG. The injector 13 is shown in FIG. 6, and detailed description thereof will be omitted. In the injector 13, one end of a communication pipe 47 is connected to the inlet 17 of the nozzle 14, and the other end of the communication pipe 47 is connected to one opening of the T-shaped connection pipe 45. Then, the communication pipe 4 is provided at the outlet 20 of the blowing portion 15 of the injector 13.
8 is connected, and the other end of the communication pipe 48 is connected to one opening of the T-shaped connecting pipe 41. Further, a communication pipe 49 is connected to the air intake port 16 of the injector 13, and the communication pipe 49 is provided with a valve 50. The other opening of the valve 50 is open to the atmosphere.

Reference numerals 51 and 51 shown in FIG. 1 are pressure gauges,
It is for measuring the pressure in each communication pipe 40, 44.

Next, a procedure for producing fresh water in which air is dissolved and dispersed by the gas-liquid mixing device having the above-mentioned structure will be described. First, the first pump 31 and the second pump 32 are sequentially driven to rotate. Then, the first pump 31 turns the fresh water 2
8 is sucked from the first suction port 35 and discharged from the first discharge port 37, and the second pump 32 sucks fresh water discharged from the first discharge port 37 from the second suction port 38 and It is discharged from the second discharge port 42. A portion of the fresh water discharged from the second discharge port 42 flows into the decompression device 33 through the communication pipe 44, is decompressed to substantially atmospheric pressure by the decompression device 33, and is discharged from the discharge pipe 46. On the other hand, a portion of the fresh water discharged from the second discharge port 42 is branched by the T-shaped connecting pipe 45 and passes through the injector 13, and the fresh water that has passed through the injector 13 flows into the T-shaped connecting pipe 41. The first discharge port 3
The second suction port 38 is merged again with the fresh water discharged from 7.
Flows into. In this way, the valve 50 of the injector 13 is opened with the fresh water flowing through the injector 13. Then, as described in the conventional example, the fresh water flowing in the injector 13 can draw in the air from the air intake port 16 of the injector 13 and take in the air, and the fresh water containing the air is ejected from the outlet 20 of the blowing unit 15. You can

In this state, the pressure of the fresh water in the flow path between the first discharge port 37 and the second discharge port 42 is set to a predetermined high pressure mainly by the first pump 31 and the second pump 32. Can be raised to. That is, since air is mixed in the second pump 32, the degree of increasing the pressure in the second pump 32 is low depending on the second pump 32. However, in the first pump 31, , The air is not mixed, and therefore the first pump 31 causes the second pump 3
The pressure in 2 can be raised to a predetermined high pressure.
Then, under a predetermined high pressure, clean water mixed with air is
Since the impeller can be stirred in the second pump 32 by the rotation of the impeller, a large amount of air can be dissolved and dispersed in fresh water.

When the fresh water, in which air is dissolved under high pressure, is decompressed by the decompression device 33 and supplied into the sewage 29 containing suspended substances under atmospheric pressure, a large number of sewage 29 is contained in the sewage 29. Ultra fine bubbles 30 are generated, and when a large number of these bubbles 30 float in the sewage 29, they adhere to many suspended substances, and the specific gravity of each suspended substance can be reduced. The suspended solids can be floated to the surface of the dirty water. The suspended matter thus floated can be efficiently separated from water and removed.

A second embodiment will be described with reference to FIG. The gas-liquid mixing apparatus of this embodiment has a second pump in the middle of a communication pipe 44 provided between the T-shaped connecting pipe 45 and the pressure reducing device 33 of the gas-liquid mixing apparatus of the first embodiment shown in FIG. A pump (spiral pump) 53 equivalent to 32 is provided.
The other points are the same as those in the first embodiment. The pump 53 has
Fresh water in which the air discharged from the second discharge port 42 of the second pump 32 is dissolved is supplied. This pump 53
Can stir the fresh water, in which the air is dissolved, by rotating the impeller to disperse the air dispersed in the fresh water more finely, and further dissolve the dispersed air in the fresh water. You can The pressure in the pump 53 can be made higher than the pressure in the second pump 32 by this pump 53, which also dissolves and disperses more air in the fresh water than in the first embodiment. be able to.

A third embodiment will be described with reference to FIG. The gas-liquid mixing apparatus of this embodiment is provided with a pump (spiral pump) 54 equivalent to the first pump 31 in the middle of the suction pipe 36 of the gas-liquid mixing apparatus of the first embodiment shown in FIG. . The other points are the same as those in the first embodiment. Pump 5
4 raises the fresh water 28 sucked through the suction pipe 36 immersed in the fresh water 28 to a predetermined water pressure, and supplies this pressurized water to the first suction port 35. As a result, the pressure in the second pump 32 can be increased more than that in the first embodiment, and as a result, more air is dissolved and dispersed in the fresh water in the second pump 32 than in the first embodiment. be able to.

A fourth embodiment will be described with reference to FIG. The gas-liquid mixing apparatus of this embodiment is the T-shaped connecting pipe 41 and the second pump 3 of the gas-liquid mixing apparatus of the first embodiment shown in FIG.
A pump (spiral pump) 55 equivalent to the second pump 32 is provided in the middle of the communication pipe 40 that communicates with the second suction port 38 of the second pump.
Is provided. The other points are the same as those in the first embodiment. According to this gas-liquid mixing device, the fresh water mixed with the air discharged from the first pump 31 is agitated while passing through the pump 55 and the second pump 32. Air can be dissolved and dispersed in fresh water, and since the pump 55 is provided, the second pump 32 can dissolve and disperse air under a higher pressure than in the first embodiment.

A fifth embodiment will be described with reference to FIG. The gas-liquid mixing apparatus of this embodiment uses a balance disk type five-stage centrifugal pump 56, which sucks fresh water 28 from a suction port 57 shown in the figure and dissolves and disperses air from a discharge port 58. Discharge high pressure fresh water. A communication pipe 59 is connected to the discharge port 58.
A decompression device 33 is provided midway. The flow passage wall 60 of the third-stage pump 67 and the flow passage wall 61 of the fifth-stage pump 69 are provided with openings 62 and 63 (see FIG. 5). 63 is made to communicate via the communicating pipes 64, 64. An injector 13 equivalent to that of the first embodiment is provided in the middle of the communication pipes 64, 64. FIG. 5 is an enlarged partial sectional view of the 5-stage centrifugal pump 56. That is, the pumps 65, 66 and 67 of the first, second and third stages of this embodiment are the first pump 31 of the first embodiment.
The pumps 68, 69 of the fourth and fifth stages are the first
It corresponds to the second pump 32 of the embodiment. The injector 13 and the communication pipes 64, 64 correspond to the gas inflow means 34 of the first embodiment. Therefore, by the first, second and third stage pumps 65, 66 and 67 which prevent air from entering,
The pressure in each of the pumps 68 and 69 of the fifth stage can be raised to a predetermined high pressure, and the pumps 68 and 69 of the fourth and fifth stages can be increased.
By rotating each impeller, air can be dissolved and dispersed in fresh water under high pressure. According to the gas-liquid mixing apparatus of the fifth embodiment, a larger amount of air can be dissolved and dispersed in fresh water than in the first embodiment. Since a multi-stage pump is used, the installation space can be reduced as compared with the case where a single-stage pump is connected and used.

A sixth embodiment will be described with reference to FIG. The difference between the gas-liquid mixing apparatus of this embodiment and the gas-liquid mixing apparatus of the fifth embodiment is that in the gas-liquid mixing apparatus of the fifth embodiment, the flow passage wall 60 of the pump 67 at the third stage and the fifth stage The openings 62 and 63 are provided in the flow path wall 61 of the eye pump 69, and these two openings 62 and 63 are communicated with each other through the communication pipes 64 and 64. The injectors are provided in the middle of these communication pipes 64 and 64. In the gas-liquid mixing apparatus of the sixth embodiment, the flow passage wall 70 of the second-stage pump 66 and the flow passage wall 71 of the fourth-stage pump 68 have openings. This 2
The two openings are communicated with each other through the communication pipes 72, 72, and the injector 13 is provided in the middle of the communication pipes 72, 72. The other points are the same as in the fifth embodiment.

A seventh embodiment will be described with reference to FIG. As shown in the figure, the gas-liquid mixing apparatus of this embodiment includes four centrifugal pumps, and the suction port 74 of the first pump 73 is connected to the suction pipe 36. And
The discharge port 76 of the first pump 73 and the suction port 78 of the second pump 77 are communicated with each other via communication pipes 79, 79, and the discharge port 80 of the second pump 77 and the third pump are connected. 81 is connected to the suction port 82 via a communication pipe 83, and the discharge port 84 of the third pump 81 and the suction port 86 of the fourth pump 85 are connected to each other via a communication pipe 87. I am doing it. At the discharge port 88 of the fourth pump 85,
A pressure reducing device 33 equivalent to that of the first embodiment is connected via a communication pipe 89, and a discharge pipe 46 is provided at the outlet of the pressure reducing device 33.
Is connected. Further, an injector 13 equivalent to that of the first embodiment is provided in the middle of the communication pipes 79, 79 that connect the first pump 73 and the second pump 77.

According to this gas-liquid mixing device, the suction pipe 36
Fresh water is sucked in through the pump, and the sucked fresh water is supplied to the first, second, third, and fourth pumps 73, 77, 81, 8 respectively.
5 can be passed in order to obtain a high pressure. Then, air can be mixed into the fresh water that is discharged from the discharge port 76, passes through the communication pipe 79, and passes through the injector 13. Second to fourth pumps 77, 81, 85
Can stir the fresh water mixed with air under high pressure by rotating each impeller to dissolve and disperse the air in the fresh water. Therefore, the decompression device 3 is used for the fresh water in which air is dissolved.
By depressurizing to approximately atmospheric pressure by 3 and discharging,
It is possible to produce fresh water in which a large number of minute bubbles are generated.

However, in the first to seventh embodiments, the injector 13 is used to mix air into the fresh water 28. However, the injector 13 is not provided and the injector 13 passes through the position corresponding to each injector 13. A configuration can be adopted in which a predetermined amount of air is forcibly mixed into fresh water. As a device for forcibly supplying air, for example, a compressor can be used. However, it is necessary to provide a flow control valve at the air discharge port of the compressor in order to adjust the amount of supplied air.

In the first to seventh embodiments, fresh water is sucked in, air is dissolved and dispersed in the fresh water,
The fresh water in which this air was dissolved was supplied to the sewage containing the suspended matter, and this suspended matter was floated on the surface of the sewage, but without sucking in the fresh water, let in the sewage to be purified,
Air may be dissolved and dispersed in this sewage, and the sewage in which this air is dissolved may be returned to the original sewage to float the suspended matter.

In the first to seventh embodiments, the gas-liquid mixing device of the present invention is used for the floating separation system in the wastewater treatment process, but it can be used for other purposes. For example, it can be applied to a cleaning device that utilizes ultrasonic waves generated when bubbles burst. In this case, air may be dissolved and dispersed in the cleaning liquid. And by generating air bubbles in the bath water, you can wash your body,
It can also be used for massage. Further, it can be used as a device for purifying lakes and marshes. Furthermore,
Carbonated water can be produced by mixing and dissolving a gas such as carbon dioxide in a liquid such as water, and is also used in a process of mixing and dissolving a gas in a liquid and chemically reacting the gas and the liquid. You can also

[0033]

The gas-liquid mixing device of the present invention can bring the pressure in the second pump to a predetermined high pressure mainly by the first pump and the second pump, and the predetermined high pressure. The configuration is such that the liquid in which gas is mixed is stirred by the impeller of the second pump below. Therefore, as compared with the first conventional example shown in FIG. 7, the pressure tank 3 can be eliminated, so that the bulk of the gas-liquid mixing device can be reduced and the structure can be simplified. As a result, there is an effect that the installation space can be reduced and the cost of the gas-liquid mixing device can be reduced. Then, as compared with the second conventional example shown in FIG. 8, the pressure in the second pump that stirs the liquid in which the gas is mixed can be made higher than the pressure in the pump 12 of the second conventional example. Amount (weight) of gas that can be dissolved and dispersed in the liquid
Can be increased as compared with the second conventional example. As a result, when the liquid in which the gas is dissolved and dispersed according to the present invention is returned to, for example, the atmospheric pressure, a large amount of bubbles can be generated as compared with the device according to the second conventional example.

The gas-liquid mixing device of the second invention uses an injector and has a structure in which gas is mixed into the liquid by the liquid passing through the injector. Therefore, as in the first conventional example shown in FIG. No need for compressor 2. Therefore, compared to the first conventional example, the compressor 2
Also, the pressure tank 3 can be dispensed with, so that the installation space of the device can be narrowed and the cost of the gas-liquid mixing device can be reduced.

[Brief description of drawings]

FIG. 1 is a front view showing a gas-liquid mixing device according to a first embodiment of the present invention.

FIG. 2 is a front view showing a gas-liquid mixing device according to second, third and fourth embodiments of the present invention.

FIG. 3 is a front view showing a gas-liquid mixing device according to fifth and sixth embodiments of the present invention.

FIG. 4 is a front view showing a gas-liquid mixing device according to a seventh embodiment of the present invention.

FIG. 5 is an enlarged partial sectional view of a five-stage centrifugal pump according to the fifth embodiment.

FIG. 6 is an enlarged cross-sectional view of the injector of the first to seventh embodiments.

FIG. 7 is a front view showing a conventional gas-liquid mixing device.

FIG. 8 is a front view showing another conventional gas-liquid mixing device.

[Explanation of symbols]

 28 Fresh water 29 Sewage 30 Air bubbles 31 First pump 32 Second pump 33 Pressure reducing device 34 Gas inflow means 35 First suction port 37 First discharge port 38 Second suction port 42 Second discharge port

Claims (2)

(57) [Claims] 1. A first pump having a first suction port for sucking in a liquid and a first discharge port for discharging the liquid sucked from the first suction port, and a first pump communicating with the first discharge port . 1
Second inlet for sucking the boosted pressure liquid body by a pump, and a second pump having a second discharge port for discharging liquid sucked from the second suction port, the second outlet port A decompression device that is provided to decompress and discharge the liquid discharged from the second discharge port, and is sucked into the second suction port.
Gas in the pressurized liquid pressurized by the first pump
A gas-liquid mixing device comprising: a gas inflow means for mixing the gas. 2. A first pump having a first suction port for sucking the liquid and a first discharge port for discharging the liquid sucked from the first suction port, and a first pump communicating with the first discharge port. A second pump having a second suction port and a second discharge port for discharging the liquid sucked from the second suction port;
A pressure reducing device provided at the discharge port for discharging the liquid discharged from the second discharge port, a communication pipe communicating the second discharge port and the second suction port, and the middle of the communication pipe And an injector capable of sucking gas from the outside of the communication pipe and entraining it in the liquid when the liquid flowing into the communication pipe from the second discharge port passes through the inside. Gas-liquid mixing device.