WO2015119204A1 - Gas-liquid mixing device and gas-liquid mixing system - Google Patents
Gas-liquid mixing device and gas-liquid mixing system Download PDFInfo
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- WO2015119204A1 WO2015119204A1 PCT/JP2015/053271 JP2015053271W WO2015119204A1 WO 2015119204 A1 WO2015119204 A1 WO 2015119204A1 JP 2015053271 W JP2015053271 W JP 2015053271W WO 2015119204 A1 WO2015119204 A1 WO 2015119204A1
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- stock solution
- liquid mixing
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/236—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids specially adapted for aerating or carbonating beverages
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
- B01F23/237—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media
- B01F23/2376—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids characterised by the physical or chemical properties of gases or vapours introduced in the liquid media characterised by the gas being introduced
- B01F23/23762—Carbon dioxide
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/421—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path
- B01F25/423—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path by means of elements placed in the receptacle for moving or guiding the components
- B01F25/4233—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions by moving the components in a convoluted or labyrinthine path by means of elements placed in the receptacle for moving or guiding the components using plates with holes, the holes being displaced from one plate to the next one to force the flow to make a bending movement
Definitions
- the present invention relates to a gas-liquid mixing apparatus and a gas-liquid mixing system.
- This application claims priority based on Japanese Patent Application No. 2014-20711 filed in Japan on February 5, 2014 and Japanese Patent Application No. 2014-134987 filed in Japan on June 30, 2014. Is hereby incorporated by reference.
- a structure using a hollow fiber membrane is known in addition to the gas mixed water generating apparatus of Patent Document 1.
- a structure using a static mixer is also known, but with this structure, the gas solubility in the stock solution cannot be increased unless the pressure is sufficiently increased. Since this is necessary, the device configuration is complicated and it is difficult to reduce the size.
- the present invention has been made in view of the above circumstances, and an object of the present invention is to enable production of a gas mixture having a relatively high solubility with a simple structure, thereby enabling downsizing and cost reduction. At the same time, it is an object to provide a gas-liquid mixing apparatus that facilitates maintenance and ensures ease of use by ensuring a sufficient flow rate, and a gas-liquid mixing system using the same.
- a gas-liquid mixing apparatus is a gas-liquid mixing apparatus for producing a gas mixed liquid by mixing a gas into a raw liquid, and the raw liquid inflow pipe into which the raw liquid continuously flows and the gas continuously
- a gas inflow pipe that flows into the gas and a liquid mixture pipe that communicates with the stock solution inflow pipe and the gas inflow pipe, respectively, and the stock solution inflow pipe and the gas inflow pipe face each other and the stock solution and the gas collide with each other.
- a gas-liquid collision part is formed, and the mixed liquid pipe is communicated with the gas-liquid collision part, and the central axis of the stock solution inflow pipe and the gas inflow pipe At least one of the central axes is arranged in a direction different from the central axis of the mixed solution pipe.
- the stock solution inflow pipe and the gas inflow pipe are communicated so that the stock solution and the gas face each other and collide with each other, thereby forming a gas-liquid collision part at this communication location, Further, the mixed liquid pipe is communicated with the gas-liquid collision portion, and at least one of the central axis of the raw liquid inlet pipe and the central axis of the gas inlet pipe is arranged in a direction different from the central axis of the mixed liquid pipe. Therefore, the stock solution flowing in from the stock solution inflow tube and the gas flowing in from the gas inflow tube collide with each other, and at least one of the central axis of the stock solution inflow tube and the central axis of the gas inflow tube is not biased to one side. Therefore, the gas mixture can be guided in different directions, so that the collision energy can be maximized with a simple structure and the solubility of the gas in the stock solution can be increased.
- the angle formed by the central axis of the stock solution inflow pipe and the central axis of the gas inflow pipe is preferably 20 ° to 180 °, more preferably 95 ° to 180 °. preferable.
- “the angle formed by the central axis of the stock solution inflow pipe and the central axis of the gas inflow tube” is the result of connecting the stock solution inflow tube and the gas inflow tube on a plane, It means the angle formed between the two central axes. According to this configuration, a gas mixture having a relatively high gas solubility can be manufactured with a simple structure.
- the stock solution is water and the gas is carbon dioxide gas. According to this configuration, carbonated water having a relatively high solubility of carbon dioxide (carbon dioxide) can be produced with a simple structure.
- a first vortex generating mechanism for generating a vortex in the gas mixture is provided in the mixture liquid pipe.
- the stock solution and the gas collide at the connection portion (the gas-liquid collision portion) of the stock solution inflow pipe and the gas inflow tube, the gas is mixed with the stock solution, and most of the gas is dissolved,
- the bubbles in the gas mixture can be refined and the specific surface area can be increased to promote dissolution in the stock solution.
- the first vortex generating mechanism is configured to face an end portion of the gas-liquid collision portion of an annular or cylindrical vortex generating portion provided in the liquid mixture pipe and the end portion. It is preferable that a groove portion formed to open to the gas-liquid collision portion side is provided between the inner wall surface of the mixed liquid pipe. According to this configuration, since the first eddy current generating mechanism includes the groove formed to open to the gas-liquid collision part side, the gas mixed liquid collides with the bottom surface of the groove and reverses the flow so that a minute amount is obtained. Eddy currents are formed, whereby the bubbles in the gas mixture are refined.
- the first vortex generating mechanism includes an upstream first vortex generating mechanism disposed on the upstream side of the mixed liquid piping, and a downstream side of the upstream first vortex generating mechanism. It is preferable that a downstream first vortex generating mechanism is provided. According to this configuration, dissolution in the stock solution can be further promoted by further miniaturizing the bubbles in the gas mixture and increasing the specific surface area, rather than providing one first vortex generating mechanism.
- a guide port that guides the gas mixture to the inner wall surface side of the downstream first vortex generating mechanism is provided in an internal hole of the vortex generating portion that constitutes the upstream first vortex generating mechanism.
- the guide port is provided in the internal hole of the vortex generating portion that constitutes the upstream first vortex generating mechanism, the gas mixture that has passed through the guide port is included in the downstream first vortex generating mechanism.
- the second vortex generating mechanism includes a narrow portion that narrows a flow path of the gas mixed liquid flowing through the mixed liquid pipe from upstream to downstream, and a flow path to a side of the narrow portion. It is preferable to have a flow path changing unit that reverses the flow of the gas mixed liquid by changing the flow rate and generates a vortex flow. According to this configuration, the gas mixture is pressurized by flowing through the narrow portion, and the solubility of the gas in the gas mixture is increased. Further, the flow of the gas mixture is reversed by the flow path changing unit, and the vortex is generated, whereby the bubbles in the gas mixture are refined and the dissolution in the stock solution is promoted.
- the said control valve is comprised by the latch type solenoid valve. According to this configuration, the power consumption of the gas-liquid mixing device having the control valve can be reduced because the latch type solenoid valve has much less power consumption than a general solenoid valve.
- the latch solenoid valve is preferably operated by a battery, and more preferably by a dry battery or a rechargeable battery.
- a dry battery or a rechargeable battery instead of a commercial power source as a power source, the usability of the gas-liquid mixing device can be improved, and for example, it can be easily used in a bathroom.
- the gas-liquid mixing system includes the gas-liquid mixing device, a raw liquid supply source that supplies the raw liquid to the raw liquid inflow pipe, a gas supply source that supplies gas to the gas inflow pipe, and the raw liquid supply source.
- a control unit that controls supply of the stock solution from the gas supply source to the stock solution inflow tube and gas supply from the gas supply source to the gas inflow tube.
- FIG. 1 It is a mimetic diagram showing a schematic structure of a 1st embodiment of a gas-liquid mixing system concerning the present invention.
- It is an external appearance perspective view which shows schematic structure of a gas-liquid mixing apparatus.
- It is a sectional side view which shows schematic structure of a gas-liquid mixing apparatus.
- It is a perspective view which shows a vortex generating member.
- It is a top view which shows a vortex generating member.
- FIG. side view which shows a vortex generating member.
- It is a perspective view which shows the other modification of a guide port.
- It is a perspective view which shows a mixing pipe.
- It is a top view which shows a mixing pipe.
- FIG. 10 is a perspective view showing an internal structure of the gas-liquid mixing system shown in FIGS. 9A to 9C.
- FIG. It is a schematic diagram which shows schematic structure of 3rd Embodiment of the gas-liquid mixing system which concerns on this invention.
- FIG. 9A to 9C It is a schematic diagram which shows schematic structure of 3rd Embodiment of the gas-liquid mixing system which concerns on this invention.
- FIG. 9C It is a schematic diagram which shows schematic structure of 3rd Embodiment of the gas-liquid mixing system which concerns on this invention.
- It is a front view which shows the external appearance of 3rd Embodiment of the gas-liquid mixing system which concerns on this invention.
- FIG. 1 is a schematic diagram showing a schematic configuration of a first embodiment of a gas-liquid mixing system according to the present invention.
- reference numeral 1 is a gas-liquid mixing system
- 2 is a gas-liquid mixing device.
- the gas-liquid mixing system 1 is for mixing and dissolving carbon dioxide (carbon dioxide) in raw water, for example, tap water, and providing the obtained carbonated water for various purposes.
- carbonated water it is used for hairdressing and beauty purposes such as shampooing, and hot water for baths, that is, carbonated springs, as in the past.
- FIG. 1 shows a schematic configuration of a gas-liquid mixing system 1 disposed in each hair wash table in a barber / beauty shop having a plurality of hair wash stands.
- the gas-liquid mixing device 2 is the first embodiment of the gas-liquid mixing device according to the present invention.
- FIG. 2A is an external perspective view of the gas-liquid mixing device 2 and a side sectional view of the gas-liquid mixing device 2.
- a raw water inflow pipe (raw liquid inflow pipe) 5 connected to the raw water supply source 3 via a pipe (raw water side pipe 30), and a pipe (gas side pipe 31) to the gas supply source 4.
- a gas inflow pipe 6 connected to each other.
- the angle shown in FIG. By setting this angle within the above range, a gas mixture having a relatively high gas solubility can be produced with a simple structure.
- the mixed liquid pipe is so arranged that the central axis of the mixed liquid pipe 8 is orthogonal to the central axis of one pipe formed by the raw water inflow pipe 5 and the gas inflow pipe 6. 8 is arranged.
- the gas inflow pipe 6 is provided with an orifice plate 6b having a small hole on the opening 6a side, so that the carbon dioxide gas supplied from the gas supply source 4 can be supplied into the gas inflow pipe 6 at a predetermined pressure. To be supplied. About the magnitude
- a mixed liquid pipe 8 is provided in the gas-liquid collision portion 7 of the raw water inflow pipe 5 and the gas inflow pipe 6 so as to communicate with the raw water inflow pipe 5 and the gas inflow pipe 6, respectively.
- a pipe main body 9 that is disposed in a direction different from the central axis of the mixed liquid pipe 8 among at least one of the central axis of the raw water inflow pipe 5 and the central axis of the gas inflow pipe 6, and is integrally connected to the gas-liquid collision unit 7;
- the housing 10 is detachably connected to the pipe body 9.
- the housing 10 is detachably connected to the pipe body 9, but the pipe body 9 and the housing 10 may be integrally formed. Further, in the present embodiment, as shown in FIG.
- ⁇ ′ is 20 ° to 180 °. It is preferably 95 ° to 180 °, more preferably 135 ° to 180 °.
- the pipe body 9 is a cylindrical body integrally connected to the gas-liquid collision part 7 between the raw water inflow pipe 5 and the gas inflow pipe 6. Therefore, the members forming the raw water inflow pipe 5, the gas inflow pipe 6, and the pipe main body 9 are integrally molded products made of resin or metal in this embodiment.
- the integrally molded product may be formed in a T-shape when viewed from the surface.
- the pipe body 9 is formed so as to surround a cylindrical guide tube 11 formed in communication with the gas-liquid collision portion 7, and therefore has an inner diameter sufficiently larger than the inner diameter of the guide tube 11. is doing.
- the housing 10 is made of a resin or metal formed in a substantially cylindrical shape, that is, in a pipe shape.
- One end side is a substantially cylindrical insertion portion 12 that is inserted into the pipe body 9, and the other end side is a pipe body 9.
- the main body 13 is a substantially cylindrical housing body 13 pulled out from the housing.
- An annular flange portion 14 is formed between the insertion portion 12 and the housing body 13. The flange portion 14 is configured to contact an annular flange 9 a provided at an end portion of the pipe body 9 when the insertion portion 12 is inserted into the pipe body 9.
- the joint clip 15 is attached to the flange portion 14 and the flange 9a as shown in FIGS. 2A and 2B.
- the flange portion 14 and the flange 9a are held and fixed in contact with each other.
- the joint clip 15 is a metal leaf spring formed in a substantially ring shape, and has an elongated opening 15a that engages with the flange portion 14 and the flange 9a along the circumferential direction thereof.
- the joint clip 15 is expanded between one end side and the other end side, and the flange portion 14 and the flange 9a are inserted into the joint clip 15. Thereafter, the end portion is closed between the other end side and the flange portion is opened in the opening 15a. 14, the flange portion 14 and the flange 9 a can be held and fixed by the joint clip 15 by engaging and projecting the flange 9 a.
- two O-rings 16, 16 are wound around the outer peripheral surface of the insertion portion 12 of the housing 10. These O-rings 16, 16 are provided so as to partially protrude in grooves (not shown) formed around the outer peripheral surface of the insertion portion 12. Under such a configuration, when the insertion portion 12 is inserted into the pipe main body 9, the O-rings 16 and 16 are interposed between the inner wall surface of the pipe main body 9 and the pipe main body 9. 9 is hermetically connected.
- a cylindrical vortex generating member (vortex generating portion) 17 is accommodated in the internal hole of such an insertion portion 12. That is, a stepped portion 12a is formed in the inner hole of the insertion portion 12 substantially at the boundary with the housing body 13 side, and the vortex generating member 17 is placed on the stepped portion 12a. As shown in FIGS. 3A to 3C, the vortex generating member 17 includes a cylindrical portion 18 and a drift plate 19 integrally formed in the cylindrical portion 18.
- 3A is a perspective view of the vortex generating member 17
- FIG. 3B is a plan view of the vortex generating member 17
- FIG. 3C is a side sectional view of the vortex generating member 17.
- the vortex generating member 17 has an upper end portion of the cylindrical portion 18, that is, an end portion on the gas-liquid collision portion 7 side, and a rear side of the central axis of the mixed liquid pipe 8 (housing 10) (gas-liquid collision portion 7 side).
- a taper surface 18a from the inside toward the outside as it goes from the front to the front side (the side opposite to the gas-liquid collision portion 7) is formed over the entire circumference of the upper end portion.
- the taper surface 18a and the surface facing the taper surface 18a that is, the inner wall surface of the mixed liquid pipe 8 (insertion portion 12 of the housing 10) facing the upper end portion of the vortex generating member 17 shown in FIG. 2B.
- a groove 20 is formed between them.
- the groove portion 20 is formed to open toward the gas-liquid collision portion 7 over the entire circumference of the upper end portion of the vortex generating member 17, and is a part of the first vortex generating mechanism in the present invention, that is, the upstream side 1 eddy current generating mechanism is configured.
- a part of the gas mixture flowing from the gas-liquid collision part 7 through the guide tube 11 and into the insertion part 12 by the groove part 20 is the bottom surface of the groove part 20, that is, the tapered surface. It collides with 18a and reverses its flow to form a minute vortex.
- size are not limited to the form shown to FIG. 3A and FIG. 3B, if it is arrange
- the form of can be adopted.
- a relatively small circular guide port 19b as shown in FIG. 4A and a plurality of smaller circular guide ports 19c as shown in FIG. 4B may be arranged.
- the guide port 19b shown in FIG. 4A and the guide port 19c shown in FIG. 4B are formed so that the total opening area thereof is substantially the same as the inner diameter of the guide tube 11 as with the guide port 19a. Is preferred. 4A and 4B show only the drift plate 19, but these drift plates 19 are provided in the cylindrical portion 18 shown in FIGS. 3A to 3C to constitute the vortex generating member 17. .
- the inner hole 21a of the large diameter portion 21 is formed in a tapered shape that gradually becomes smaller in diameter toward the small diameter portion 22 side.
- the lower end side that is, the side communicating with the inner hole 22a of the small diameter portion 22 is a tapered surface 21b having a large inclination angle (taper angle) formed by the inner wall surface. That is, the tapered surface 21b is formed to be inclined with respect to the central axis (not shown) so as to go from the outside to the inside as it goes to the small diameter portion 22 side.
- a groove portion 24 is formed between the upper end portion of the mixing pipe 23 and the inner wall surface (housing main body 13 of the housing 10) of the mixed liquid pipe 8 facing the upper end portion, that is, the tapered surface 21b. Yes.
- the groove portion 24 is formed to open to the gas-liquid collision portion 7 side, that is, the vortex generating member 17 side constituting the upstream first vortex generating mechanism over the entire circumference of the upper end portion of the mixing pipe 23,
- the downstream 1st eddy current generation mechanism used as a part of the 1st eddy current generation mechanism in this invention is comprised.
- the first vortex flow is generated by such a downstream first vortex generating mechanism having the mixing pipe 23 as a vortex generating portion and the upstream first vortex generating mechanism having the vortex generating member 17 as a vortex generating portion.
- a generation mechanism is configured.
- the upper end of the mixing pipe 23 constitutes a downstream first vortex generating mechanism, but in the present embodiment, a second vortex generating mechanism is formed inside thereof separately from this. That is, the mixing pipe 23 has a narrow portion 25 and a flow path changing portion 26 inside as shown in FIGS. 5A to 5C.
- 5A is a perspective view of the mixing pipe 23
- FIG. 5B is a plan view of the mixing pipe 23
- FIG. 5C is a side sectional view of the mixing pipe 23.
- the narrow portion 25 is provided with a first baffle plate 27 a extending from a part of the inner wall surface of the mixing pipe 23 toward the center side. This is an opening formed between the tip of the baffle plate 27 a and the inner wall surface of the mixing pipe 23. As described above, since the inner hole of the mixing pipe 23 is partially closed by the first baffle plate 27a, the remaining opening portion inevitably narrows the opening area, so that the flow path of the gas mixture can be made upstream. It becomes the site
- a second baffle plate 27b extends from another part of the inner wall surface of the mixing pipe 23 toward the center side. Is provided. Since the second baffle plate 27b is arranged directly under the narrow portion 25 in this way, the gas mixture flowing through the narrow portion 25 collides with the second baffle plate 27b, and then the second baffle plate 27b. It flows through an opening 27 c formed between the tip of the mixing pipe 23 and the inner wall surface of the mixing pipe 23. Accordingly, the second baffle plate 27b and the opening 27c formed on the tip side of the second baffle plate 27b constitute a flow path changing portion 26 that changes the flow path to the side of the narrow portion 25.
- the mixing pipe 23 is formed with two notches 28a and 28b on the side wall as shown in FIGS. 5A and 5C. These notches 28a and 28b are mainly used for forming the first baffle plate 27a and the second baffle plate 27b. Moreover, the annular fitting convex part fitted to the fitting recessed part (not shown) formed in the lower end part of the small diameter part 22 of the housing main body 13 as shown in FIG. 2B at the lower end part of the mixing pipe 23 29 is formed. The fitting pipe 29 is detachably fitted into the fitting recess at the lower end of the small-diameter portion 22, so that the mixing pipe 23 is detachably accommodated in the housing body 13.
- the mixing pipe 23 accommodated and fixed in the housing body 13 in this way has an opening on the lower end side serving as a gas mixture jet outlet of the gas-liquid mixing device 2. Therefore, although not shown, the hose and the shower head are attached to the small diameter portion 22 of the housing body 13. Therefore, the small diameter portion 22 has a male screw portion (not shown) formed on the outer peripheral surface thereof, and a hose is detachably attached thereto.
- the raw water supply source 3 is a water pipe, and therefore, the raw water side pipe 30 is disposed between the water pipe and the raw water inflow pipe 5.
- the water pipe or the raw water inflow pipe 5 may be provided with a heating device (not shown) for heating the tap water to a predetermined temperature, for example, a preset temperature of about 30 ° C. to 45 ° C. .
- a heating device not shown
- the temperature within the above temperature range, preferably about 35 ° C. to 40 ° C.
- a predetermined amount of sodium chloride may be dissolved in tap water as raw water in advance to obtain physiological saline for medical purposes. Furthermore, you may add the fragrance
- the raw water supply source 3 various water sources can be used in addition to the water pipe.
- the gas supply source 4 in this embodiment, a gas cylinder filled with carbon dioxide gas at a pressure (gauge pressure) of about 0.5 MPa is used.
- the raw water side pipe 30 is provided with a first pressure switch 32 serving as a pressure switch of the present invention.
- the first pressure switch 32 reduces the pressure of the raw water flowing in the raw water side pipe 30 (in the raw water inflow pipe 5) without narrowing the flow path of the raw water side pipe 30, that is, the raw water inflow pipe 5.
- This is a sensor to detect, and has a known configuration in which a switch is turned on when a predetermined pressure higher than a preset pressure is detected and the switch is turned off when the pressure is lower than a predetermined pressure.
- the first pressure switch 32 is electrically connected to the control unit 40, and transmits a detected on / off signal to the control unit 40.
- the gas side pipe 31 connected to the gas side supply pipe 6 of the gas-liquid mixing apparatus 2 shown in FIGS. 6A and 6B includes an electromagnetic valve 33 in the path between the gas supply source 4 as shown in FIG. (Control valve) and a second pressure switch 34 are provided.
- the second pressure switch 34 is disposed on the gas supply source 4 side, detects the pressure of the carbon dioxide gas flowing through the gas side pipe 31, and is equal to or higher than a preset pressure (for example, 0.3 MPa [gauge pressure]). If so, the switch is turned on, and if it is less than a preset pressure, the switch is turned off. Therefore, the second pressure switch 34 functions as a fuel gauge for determining the residual pressure in the gas cylinder constituting the gas supply source 4, that is, the remaining amount of carbon dioxide in the gas cylinder.
- a preset pressure for example, 0.3 MPa [gauge pressure]
- the second pressure switch 34 is also electrically connected to the control unit 40, and transmits an on / off signal based on the detection result to the control unit 40.
- the control unit 40 whether or not the detection result of the second pressure switch 34, that is, the remaining amount of the gas supply source 4 (gas cylinder) is equal to or higher than a preset pressure (amount) is displayed on the display unit of the operation panel (not shown). Is displayed.
- the electromagnetic valve 33 is disposed on the downstream side of the second pressure switch 34 and adjusts the supply of carbon dioxide from the gas supply source 4 by opening and closing thereof. That is, when the electromagnetic valve 33 is opened, carbon dioxide is supplied from the gas supply source 4 to the gas inflow pipe 6 of the gas-liquid mixing device 2, and when closed, the supply of carbon dioxide is stopped.
- the opening and closing of the electromagnetic valve 33 is controlled by being electrically connected to the control unit 40.
- the control unit 40 receives the on / off signal from the first pressure switch 32 and controls the opening / closing of the electromagnetic valve 33 based on the on / off signal. That is, the first pressure switch 32 detects that the pressure in the raw water side pipe 30 (raw water inflow pipe 5) is equal to or higher than a predetermined pressure, and therefore the raw water is flowing at a predetermined flow rate or higher, and controls the ON signal. When transmitting to the unit 40, the control unit 40 transmits an ON signal to the electromagnetic valve 33 in order to open the electromagnetic valve 33. Then, the electromagnetic valve 33 is opened, and carbon dioxide gas is supplied to the gas-liquid mixing device 2.
- the pressure in the raw water side pipe 30 (raw water inflow pipe 5 control unit 40) is less than a predetermined pressure, and therefore the first pressure switch 32 cannot detect that the raw water is flowing at a predetermined flow rate or higher. In this case, the ON signal is not transmitted to the control unit 40, and thus the control unit 40 closes the electromagnetic valve 33 without opening it. Then, since the electromagnetic valve 33 is closed, the carbon dioxide gas is not supplied to the gas-liquid mixing device 2.
- carbon dioxide gas is supplied to the gas-liquid mixing device 2 only when the raw water flows at a predetermined flow rate or higher and is supplied to the gas-liquid mixing device 2, so that the carbon dioxide gas is excessive. Consumption is prevented, and the gas mixture to be produced, that is, the carbon dioxide concentration in the carbonated water is adjusted to an appropriate range set in advance.
- the control unit 40 includes a CPU, a memory device, and the like, and has an operation panel that also functions as a display unit.
- the entire gas-liquid mixing system 1 is turned on and off, and various data are output via the operation panel. Can be done. That is, the control unit 40, based on the signals from the first pressure switch 32 and the second pressure switch 34 described above, supply time (supply amount) of raw water, supply time (supply amount) of carbon dioxide gas, The remaining amount of carbon dioxide gas from the gas supply source 4 is calculated.
- the various information calculated in this way can be output to an external terminal such as an iOS terminal or an Android via the output unit 35 in the control unit 40.
- an external terminal such as an iOS terminal or an Android
- the output part 35 what is output by communication means (for example, Bluetooth (trademark) etc.) which is not illustrated is provided.
- a tablet, a smartphone, or the like is preferably used, and various information calculated by the control unit 40 can be easily received.
- a hairdressing and beauty shop having a plurality of hair basins as in the present embodiment, when the gas-liquid mixing system 1 is disposed in each basin, various information is output from the gas-liquid mixing system 1 of each basin. Various information can be input to one external terminal. Therefore, the person in charge of the hairdressing and beauty shop can easily check the operating status of each hair basin, the past driving history, and the like by looking at the external terminal to which various information has been input.
- water hot water
- tap water as the raw water supply source 3
- a predetermined pressure set in advance, for example, 0.10 to 0.20 MPa, preferably 0.10 to 0.15 MPa (gauge pressure).
- Flow in side pipe 30 By supplying the raw water at such a predetermined pressure, in this embodiment, the flow rate is set to be, for example, about 6 to 15 l / min, preferably about 6 to 10 l / min.
- the first pressure switch 32 detects this and opens the electromagnetic valve 33 via the control unit 40.
- the second pressure switch 34 detects the remaining pressure (remaining amount) in the gas supply source (gas cylinder) 4 and displays the result on the operation panel of the control unit 40. Therefore, if the residual pressure of the gas supply source 4 is equal to or higher than a preset pressure, the operator proceeds with the production of carbonated water as it is. Moreover, when the residual pressure of the gas supply source 4 is less than a preset pressure, the gas supply source 4 is exchanged as necessary.
- the gas supply source (gas cylinder) 4 is provided with a pressure regulator and a pressure gauge. For example, the replacement timing of the gas supply source 4 can be determined by checking the pressure gauge.
- Carbon dioxide gas that has passed through the solenoid valve 33 is adjusted to have a flow rate of, for example, about 4 to 12 l / min, preferably about 5 to 11 l / min, by a flow rate regulator (not shown) provided on the upstream side or downstream side of the solenoid valve 33. Adjusted to When raw water is supplied from the raw water supply source 3 to the raw water inflow pipe 5 via the raw water side pipe 30, and carbon dioxide is supplied from the gas supply source 4 to the gas inflow pipe 6 via the gas side pipe 31, FIG. The raw water and carbon dioxide gas (gas) collide at the gas-liquid collision part 7 and are mixed as indicated by arrows in FIG. Then, it flows into the mixed liquid pipe 8 through the guide pipe 11.
- a flow rate regulator not shown
- the raw water and the carbon dioxide gas collide with each other in the gas-liquid collision unit 7, and the gas mixture obtained in a direction different from at least one of the raw water and the carbon dioxide gas without being biased to one side is guided,
- the collision energy is maximized, the carbon dioxide is sufficiently mixed with the raw water, and the solubility of the carbon dioxide in the raw water is increased.
- the saturated concentration of carbon dioxide with respect to water at a temperature of 40 ° C. is about 1000 ppm.
- the gas-liquid mixing unit 2 after colliding with the gas-liquid collision unit 7, the gas-liquid mixing unit 2 passes through the guide tube 11 by flowing into the mixed solution pipe 8 through the guide tube 11.
- the concentration of carbon dioxide in the gas mixture could be adjusted to about 800 to 850 ppm.
- natural water exists as a state which became a bubble and was mixed in the gas liquid mixture.
- the gas mixed solution (carbonated water) that has flowed into the mixed solution pipe 8 flows toward the vortex generating member 17 provided in the insertion portion 12 of the housing 10. At that time, a part of the gas mixture liquid flows toward the groove portion 20 (upstream first vortex generating mechanism) provided between the upper end portion of the vortex generating member 17 and the inner wall surface of the insertion portion 12. As shown by the arrows in FIG. 7, a minute vortex is generated. That is, the gas mixed solution collides with the bottom surface (tapered surface 18 a) of the groove portion 20, reverses the flow thereof, and flows in a direction intersecting with the central axis of the mixed solution pipe 8, thereby generating a minute vortex.
- the bubbles in the gas mixture are refined and the specific surface area is increased.
- the contact area of the carbon dioxide gas which forms a bubble, and gas mixed liquid (raw water) increases, and melt
- the gas mixture whose carbon dioxide concentration is increased by the upstream first vortex generating mechanism passes through the guide port 19a of the drift plate 19 of the vortex generating member 17, as indicated by an arrow in FIG. And flows on the inner wall surface side of the inner hole 21 a of the large-diameter portion 21 of the housing body 13.
- most of the gas mixture is a groove portion 24 (downstream first vortex generating mechanism) provided between the inner wall surface of the inner hole 21 a of the large diameter portion 21, that is, the tapered surface 21 b, and the upper end portion of the mixing pipe 23.
- a minute vortex is generated as shown by an arrow in FIG. That is, the gas mixed liquid collides with the bottom surface (tapered surface 21 b) of the groove portion 24, reverses the flow thereof, and flows in a direction intersecting with the central axis of the mixed liquid piping 8, thereby generating a minute vortex.
- the gas mixture that has flowed into the mixing pipe 23 is pressurized by flowing through the narrow portion 25 as shown in FIG. 5C, thereby increasing the solubility of the carbon dioxide gas in the gas mixture.
- the flow is reversed by the second baffle plate 27 b and flows in a direction crossing the central axis of the mixed liquid pipe 8, thereby generating a vortex.
- eddy_current is produced also when a flow path is changed toward the opening 27c after that.
- bubbles in the gas mixture are refined, and dissolution of carbon dioxide in the gas mixture (raw water) is promoted.
- the gas mixture is increased to a carbon dioxide concentration of about 1000 ppm, which is a saturated concentration.
- the gas-liquid mixed solution (carbonated water) in which carbon dioxide gas is dissolved to a saturation concentration in this way is supplied to a hose connected to the small diameter portion 22 of the housing body 13 and a shower head provided at the tip of the hose. It is made to erupt through and is used for hair washing.
- the gas-liquid mixing device 2 of the present embodiment causes the raw water supplied by the raw water inflow pipe 5 and the carbon dioxide gas (gas) supplied by the gas inflow pipe 4 to collide with each other, and the mixed liquid Since the gas mixture is guided in a direction different from at least one of the raw water and carbon dioxide without being biased to one side by the pipe 8, the collision energy is maximized with a simple structure and the solubility of carbon dioxide in the raw water is increased. Can do. Accordingly, a driving source such as a pump is not required, and carbonated water having a relatively high solubility can be produced with a simple structure. This makes it possible to reduce the size and cost of the gas-liquid mixing device. .
- the first eddy current generating mechanism includes grooves 20 and 24 formed between the upper end portion of the vortex generating portion including the vortex generating member 17 and the mixing pipe 23 and the inner wall surface of the mixed liquid pipe 8 facing the upper end portion. Therefore, by causing the gas mixture to collide with the bottom surfaces of the groove portions 20 and 24 and reversing the flow, a fine vortex can be formed and the bubbles in the gas mixture can be miniaturized. Therefore, the dissolution of carbon dioxide in the raw water (gas mixture) can be promoted.
Abstract
Description
本願は、2014年2月5日に日本に出願された特願2014-20711号及び2014年6月30日に日本に出願された特願2014-134987号に基づき優先権を主張し、その内容をここに援用する。 The present invention relates to a gas-liquid mixing apparatus and a gas-liquid mixing system.
This application claims priority based on Japanese Patent Application No. 2014-20711 filed in Japan on February 5, 2014 and Japanese Patent Application No. 2014-134987 filed in Japan on June 30, 2014. Is hereby incorporated by reference.
また、スタティックミキサを用いた構造のものも知られているが、この構造のものでは充分に圧を上げないと原液に対する気体の溶解度を高めることができず、したがって通常はポンプ等の駆動原が必要になるため、装置構成が複雑になって小型化が難しくなっている。 As a structure for dissolving the carbon dioxide gas, a structure using a hollow fiber membrane is known in addition to the gas mixed water generating apparatus of Patent Document 1. However, it is difficult to secure the flow rate, to reduce the size, and to reduce the price of the one using the hollow fiber membrane.
A structure using a static mixer is also known, but with this structure, the gas solubility in the stock solution cannot be increased unless the pressure is sufficiently increased. Since this is necessary, the device configuration is complicated and it is difficult to reduce the size.
この構成によれば、気体の溶解度が比較的高い気体混合液を簡易な構造で製造することができる。 In the gas-liquid mixing apparatus, the angle formed by the central axis of the stock solution inflow pipe and the central axis of the gas inflow pipe is preferably 20 ° to 180 °, more preferably 95 ° to 180 °. preferable. Here, "the angle formed by the central axis of the stock solution inflow pipe and the central axis of the gas inflow tube" is the result of connecting the stock solution inflow tube and the gas inflow tube on a plane, It means the angle formed between the two central axes.
According to this configuration, a gas mixture having a relatively high gas solubility can be manufactured with a simple structure.
この構成によれば、炭酸ガス(二酸化炭素)の溶解度が比較的高い炭酸水を簡易な構造で製造することができる。 In the gas-liquid mixing apparatus, it is preferable that the stock solution is water and the gas is carbon dioxide gas.
According to this configuration, carbonated water having a relatively high solubility of carbon dioxide (carbon dioxide) can be produced with a simple structure.
この構成によれば、原液流入管と気体流入管の接続部(前記の気液衝突部)で原液と気体とが衝突し、原液に気体が混合してその多くが溶解した気体混合液に、渦流を生じさせることにより、気体混合液中の気泡を微細化し、その比表面積を大きくすることで原液に対する溶解を促進することができる。 In the gas-liquid mixing apparatus, it is preferable that a first vortex generating mechanism for generating a vortex in the gas mixture is provided in the mixture liquid pipe.
According to this configuration, the stock solution and the gas collide at the connection portion (the gas-liquid collision portion) of the stock solution inflow pipe and the gas inflow tube, the gas is mixed with the stock solution, and most of the gas is dissolved, By causing the vortex to flow, the bubbles in the gas mixture can be refined and the specific surface area can be increased to promote dissolution in the stock solution.
この構成によれば、第1渦流生成機構が気液衝突部側に開口して形成された溝部を備えているので、気体混合液が溝部の底面に衝突してその流れを反転させることで微小な渦流を形成し、これによって気体混合液中の気泡が微細化する。 Further, in the gas-liquid mixing apparatus, the first vortex generating mechanism is configured to face an end portion of the gas-liquid collision portion of an annular or cylindrical vortex generating portion provided in the liquid mixture pipe and the end portion. It is preferable that a groove portion formed to open to the gas-liquid collision portion side is provided between the inner wall surface of the mixed liquid pipe.
According to this configuration, since the first eddy current generating mechanism includes the groove formed to open to the gas-liquid collision part side, the gas mixed liquid collides with the bottom surface of the groove and reverses the flow so that a minute amount is obtained. Eddy currents are formed, whereby the bubbles in the gas mixture are refined.
この構成によれば、第1渦流生成機構を一つ設けるよりも、気体混合液中の気泡をさらに微細化し、その比表面積を大きくすることで原液に対する溶解をさらに促進することができる。 Further, in the gas-liquid mixing apparatus, the first vortex generating mechanism includes an upstream first vortex generating mechanism disposed on the upstream side of the mixed liquid piping, and a downstream side of the upstream first vortex generating mechanism. It is preferable that a downstream first vortex generating mechanism is provided.
According to this configuration, dissolution in the stock solution can be further promoted by further miniaturizing the bubbles in the gas mixture and increasing the specific surface area, rather than providing one first vortex generating mechanism.
この構成によれば、上流側第1渦流生成機構を構成する渦発生部の内部孔に案内口を設けているので、該案内口を通った気体混合液が下流側第1渦流生成機構の内壁面側に案内されることで該下流側第1渦流生成機構の溝部の底面により多く衝突し、流れを反転して渦流を形成することで気体混合液中の気泡が微細化する。 In addition, a guide port that guides the gas mixture to the inner wall surface side of the downstream first vortex generating mechanism is provided in an internal hole of the vortex generating portion that constitutes the upstream first vortex generating mechanism. Preferably it is.
According to this configuration, since the guide port is provided in the internal hole of the vortex generating portion that constitutes the upstream first vortex generating mechanism, the gas mixture that has passed through the guide port is included in the downstream first vortex generating mechanism. By being guided to the wall surface side, more collisions are made with the bottom surface of the groove portion of the downstream first vortex generating mechanism, and the flow is reversed to form a vortex, whereby the bubbles in the gas mixture are refined.
この構成によれば、原液流入管と気体流入管の接続部(前記の気液衝突部)で原液と気体とが衝突し、原液に気体が混合してその多くが溶解した気体混合液を、渦流を生じさせることにより、気体混合液中の気泡を微細化し、その比表面積を大きくすることで原液に対する溶解を促進することができる。また、混合液配管を流れる気体混合液の流路を上流から下流に向けて狭めるようにしたので、気体混合液を加圧することによって該気体混合液中への気体の溶解度を高めることができる。 Further, in the gas-liquid mixing apparatus, the mixture liquid pipe is configured to generate a vortex in the gas mixture liquid by narrowing a flow path of the gas mixture liquid flowing through the mixture liquid pipe from upstream to downstream. It is preferable that a two-eddy current generating mechanism is provided.
According to this configuration, the stock solution and the gas collide at the connection portion (the gas-liquid collision portion) of the stock solution inflow pipe and the gas inflow tube, and the gas mixture solution in which the gas is mixed and dissolved in the stock solution, By causing the vortex to flow, the bubbles in the gas mixture can be refined and the specific surface area can be increased to promote dissolution in the stock solution. Moreover, since the flow path of the gas mixed liquid flowing through the mixed liquid piping is narrowed from the upstream toward the downstream, the gas solubility in the gas mixed liquid can be increased by pressurizing the gas mixed liquid.
この構成によれば、狭隘部を流れることで気体混合液が加圧され、該気体混合液中での気体の溶解度が高まる。また、流路変更部によって気体混合液の流れが反転し、渦流が生じることにより、気体混合液中の気泡が微細化して原液に対する溶解が促進される。 Further, in the gas-liquid mixing apparatus, the second vortex generating mechanism includes a narrow portion that narrows a flow path of the gas mixed liquid flowing through the mixed liquid pipe from upstream to downstream, and a flow path to a side of the narrow portion. It is preferable to have a flow path changing unit that reverses the flow of the gas mixed liquid by changing the flow rate and generates a vortex flow.
According to this configuration, the gas mixture is pressurized by flowing through the narrow portion, and the solubility of the gas in the gas mixture is increased. Further, the flow of the gas mixture is reversed by the flow path changing unit, and the vortex is generated, whereby the bubbles in the gas mixture are refined and the dissolution in the stock solution is promoted.
この構成によれば、原液流入管に、その流路を狭めることなく該流路を流れる原液の圧力を検知する圧力スイッチを設けているので、原液の流路が狭められることで加圧され、その流量が絞られて所望の流量の気体混合液が得られなくなるのを防止することができる。 Further, in the gas-liquid mixing apparatus, the stock solution inflow pipe has a pressure switch for detecting that the pressure of the stock solution flowing through the flow path is not less than a predetermined pressure without narrowing the flow path of the stock solution inflow pipe. The gas inflow pipe is provided with a control valve provided between the gas inflow pipe and the gas supply source to control the supply of gas from the gas supply source to the gas inflow pipe, and the pressure The switch is preferably configured to open the control valve when it is detected that the pressure of the stock solution has become equal to or higher than a predetermined pressure.
According to this configuration, the stock solution inflow pipe is provided with a pressure switch that detects the pressure of the stock solution flowing through the flow path without narrowing the flow path. It can be prevented that the flow rate is reduced and a gas mixture having a desired flow rate cannot be obtained.
この構成によれば、ラッチ式電磁弁が一般の電磁弁に比べて消費電力が格段に少ないことにより、制御弁を有する気液混合装置の消費電力を少なくすることができる。 Moreover, in the said gas-liquid mixing apparatus, it is preferable that the said control valve is comprised by the latch type solenoid valve.
According to this configuration, the power consumption of the gas-liquid mixing device having the control valve can be reduced because the latch type solenoid valve has much less power consumption than a general solenoid valve.
電源として商用電源に代えて、乾電池や充電池を用いることにより、気液混合装置の使い勝手を良くし、例えば風呂場での使用を容易にすることができる。 In the gas-liquid mixing device, the latch solenoid valve is preferably operated by a battery, and more preferably by a dry battery or a rechargeable battery.
By using a dry battery or a rechargeable battery instead of a commercial power source as a power source, the usability of the gas-liquid mixing device can be improved, and for example, it can be easily used in a bathroom.
この構成によれば、制御弁として比例電磁弁を用いているので、調整部によってこの比例電磁弁の開度を切り換えることにより、気体供給源から気体流入管への気体の供給量を調整することができる。したがって、原液流入管から流入する原水に対して、気体の流量を調整することにより、得られる気液混合液の濃度を異なる複数の濃度に調整することができる。 Further, in the gas-liquid mixing apparatus, the control valve is constituted by a proportional solenoid valve, and the proportional solenoid valve has an adjustment unit that adjusts a gas supply amount from the gas supply source to the gas inflow pipe. It is preferable to be provided.
According to this configuration, since the proportional solenoid valve is used as the control valve, the amount of gas supplied from the gas supply source to the gas inflow pipe is adjusted by switching the opening of the proportional solenoid valve by the adjusting unit. Can do. Therefore, the concentration of the gas-liquid mixture obtained can be adjusted to a plurality of different concentrations by adjusting the gas flow rate with respect to the raw water flowing from the raw solution inflow pipe.
この気液混合システムでは、前記の気液混合装置を備えることにより、簡易な構造で原液に対する気体の溶解度を高めることができる。したがって、小型化や低価格化を可能にするとともに、メンテナンスを容易にし、充分な流量を確保することで使い勝手を良くすることができる。 The gas-liquid mixing system according to the present invention includes the gas-liquid mixing device, a raw liquid supply source that supplies the raw liquid to the raw liquid inflow pipe, a gas supply source that supplies gas to the gas inflow pipe, and the raw liquid supply source. A control unit that controls supply of the stock solution from the gas supply source to the stock solution inflow tube and gas supply from the gas supply source to the gas inflow tube.
In this gas-liquid mixing system, by providing the gas-liquid mixing device, the solubility of the gas in the stock solution can be increased with a simple structure. Therefore, it is possible to reduce the size and price, facilitate maintenance, and improve usability by securing a sufficient flow rate.
図1は、本発明に係る気液混合システムの第1実施形態の概略構成を示す模式図であり、図1中符号1は気液混合システム、2は気液混合装置である。 Hereinafter, a gas-liquid mixing apparatus and a gas-liquid mixing system according to the present invention will be described in detail with reference to the drawings.
FIG. 1 is a schematic diagram showing a schematic configuration of a first embodiment of a gas-liquid mixing system according to the present invention. In FIG. 1, reference numeral 1 is a gas-liquid mixing system, and 2 is a gas-liquid mixing device.
原水流入管5及び気体流入管6の形状及び寸法については、前記したような本発明の効果を損なわない限り特に制限はないが、円筒形であることが好ましい。
また、原水流入管5の中心軸と気体流入管6の中心軸のうちのいずれかと混合液配管8の中心軸との間で形成される角度が10°~90°であることが好ましく、45°~90°であることがより好ましい。なお、この角度は、原水流入管5と気体流入管6のうちのいずれかと混合液配管8が連結された状態のものを平面上に配置した場合に、前記2つの中心軸の間に形成される角度を意味する。例えば、原水流入管5の中心軸と混合液配管8の中心軸との間で形成される角度の場合、図13に示す角度がθである。この角度を上記の範囲とすることにより、気体の溶解度が比較的高い気体混合液を簡易な構造で製造することができる。図2A及び図2Bに示す態様においては、原水流入管5と気体流入管6とにより形成される一つの配管の中心軸に対して、混合液配管8の中心軸が直交するように混合液配管8が配置されている。
なお、気体流入管6には、その開口6a側に小孔を有するオリフィス板6bが設けられており、これによって気体供給源4から供給される炭酸ガスは、所定の圧力で気体流入管6内に供給されるようになっている。この小孔の大きさや数については、所望の気体圧力に応じて適宜選択することができる。 In this embodiment, the raw
The shapes and dimensions of the raw
The angle formed between any one of the central axis of the raw
The
本実施形態では、ハウジング10が配管本体9に着脱可能に連結しているが、配管本体9とハウジング10とが一体に形成されていてもよい。
また、本実施形態では、図13に示すように、原前記原液流入管の中心軸と前記気体流入管の中心軸とのなす角度をθ’とすると、θ’は20°~180°であることが好ましく、95°~180°であることがより好ましく、135°~180°であることが特に好ましい。このように構成することにより、気体の溶解度が比較的高い気体混合液を簡易な構造で製造することができる。
また、本発明の装置において、原水流入管5、気体流入管6及び混合液配管8のそれぞれの中心軸は、これらを同一平面上に配置できるように構成されていても、これらが三角錐を形成するように構成されていても良い。 Further, a mixed
In the present embodiment, the
Further, in the present embodiment, as shown in FIG. 13, if the angle between the central axis of the raw solution inflow pipe and the central axis of the gas inflow pipe is θ ′, θ ′ is 20 ° to 180 °. It is preferably 95 ° to 180 °, more preferably 135 ° to 180 °. By comprising in this way, the gas liquid mixture whose gas solubility is comparatively high can be manufactured with a simple structure.
In the apparatus of the present invention, the central axes of the raw
本実施形態では、このようなミキシングパイプ23を渦発生部とする下流側第1渦流生成機構と、渦発生部材17を渦発生部とする前記上流側第1渦流生成機構とにより、第1渦流生成機構が構成されている。 As described later, a large amount of the gas mixture flowing into the
In the present embodiment, the first vortex flow is generated by such a downstream first vortex generating mechanism having the mixing
また、ミキシングパイプ23の下端部には、図2Bに示すようにハウジング本体13の小径部22の下端部に形成された嵌合凹部(図示せず)に嵌合する円環状の嵌合凸部29が形成されている。この嵌合凸部29が小径部22の下端部の嵌合凹部に着脱可能に嵌合させられることにより、ミキシングパイプ23はハウジング本体13内に着脱可能に収容固定されている。 The mixing
Moreover, the annular fitting convex part fitted to the fitting recessed part (not shown) formed in the lower end part of the
一方、気体供給源4としては、本実施形態では炭酸ガスを0.5MPa程度の圧(ゲージ圧)で充填したガスボンベが用いられる。 In addition to heating in this manner, for example, a predetermined amount of sodium chloride may be dissolved in tap water as raw water in advance to obtain physiological saline for medical purposes. Furthermore, you may add the fragrance | flavor as needed. As the raw
On the other hand, as the
図6A、図6Bに示した気液混合装置2の気体側供給管6に接続する気体側配管31には、図1に示すように気体供給源4との間の経路中に、電磁弁33(制御弁)と第2の圧力スイッチ34とが設けられている。 As shown in FIG. 1, the
The
まず、原水供給源3である水道から水(湯)を、予め設定された所定の圧力、例えば0.10~0.20MPa、好ましくは0.10~0.15MPaの圧(ゲージ圧)で原水側配管30に流す。このような所定の圧力で原水を供給することにより、本実施形態ではその流量が、例えば6~15l/分、好ましくは6~10l/分程度となるように設定されている。 Next, the production of carbonated water to be a gas mixture by the gas-liquid mixing system 1 (gas-liquid mixing device 2) having such a configuration will be described.
First, water (hot water) is supplied from tap water as the raw
気体供給源4側では、第2の圧力スイッチ34が気体供給源(ガスボンベ)4内の残圧(残量)を検知し、制御部40の操作パネルにその結果を表示させる。したがって、操作者は気体供給源4の残圧が予め設定された圧以上であれば、そのまま炭酸水の製造を進める。また、気体供給源4の残圧が予め設定された圧未満である場合には、必要に応じて気体供給源4の交換などを行う。なお、気体供給源(ガスボンベ)4には圧力調整器や圧力計が備えられており、例えば圧力計を確認することで、気体供給源4の交換時期を決定することもできる。 When the raw water is flowed in this way and the inside of the raw
On the
原水供給源3から原水側配管30を介して原水流入管5に原水が供給され、気体供給源4から気体側配管31を介して気体流入管6に炭酸ガスが供給されると、図7中に矢印で示すように原水と炭酸ガス(気体)とが気液衝突部7にて衝突し、混合される。そして、案内管11を通って混合液配管8内に流入する。 Carbon dioxide gas that has passed through the
When raw water is supplied from the raw
下流側第1渦流生成機構(溝部24)で炭酸ガス濃度が高められた気体混合液は、図7中に矢印で示すように、ミキシングパイプ23内に流入する。 By generating such a small vortex, the dissolution of carbon dioxide in the gas mixture (raw water) is promoted in the same manner as in the groove 20 (upstream first vortex generation mechanism). The gas concentration is further increased.
The gas mixture whose carbon dioxide concentration is increased by the downstream first vortex generating mechanism (groove portion 24) flows into the mixing
このように気体混合液の流路を上流から下流に向けて狭める狭隘部25を有した第2渦流生成機構を省略することにより、得られる炭酸水(気体混合液)の炭酸ガス(気体)の溶解度は低くなるものの、狭隘部25による気体混合液の加圧を無くすことで流量が絞られることを抑えることができ、したがって得られる炭酸水(気体混合液)の流量を多くすることができる。 Therefore, by replacing and fixing such a
Thus, by omitting the second eddy current generating mechanism having the
図9A~図9Cは、本発明に係る気液混合システムの第2実施形態の概略構成を示す図であり、図9Aは外観を示す正面図、図9Bは内部構造を示す正面図、図9Cは外観を示す背面図である。また、図10は図9A~図9Cに示した気液混合システムの内部構造を示す斜視図である。図9A~図9Cにおいて符号50は気液混合システムであり、この気液混合システム50は、筐体51内に前記実施形態で示した本発明に係る前記気液混合装置2や、これに付随する各種構成要素をコンパクトに収容したものである。 Next, a second embodiment of the gas-liquid mixing apparatus and gas-liquid mixing system according to the present invention will be described. In the following description, the same components as those in the first embodiment are denoted by the same reference numerals, and the description thereof is omitted.
9A to 9C are diagrams showing a schematic configuration of a second embodiment of the gas-liquid mixing system according to the present invention, FIG. 9A is a front view showing an appearance, FIG. 9B is a front view showing an internal structure, and FIG. FIG. 3 is a rear view showing an appearance. FIG. 10 is a perspective view showing the internal structure of the gas-liquid mixing system shown in FIGS. 9A to 9C. 9A to 9C,
また、使用後はON/OFFのための表示55を再度押圧することにより、気液混合装置2の作動を停止させることができる。 Therefore, the operator can confirm that carbonated water is ejected from the small-
Moreover, the operation of the gas-
第3実施形態が第2実施形態と異なるところは、図9B、図10に示した制御弁52として、ラッチ式電磁弁に代えて比例電磁弁を用いた点である。比例電磁弁は、一般の電磁弁のようにその流路の開度を単に「開/閉」の二段階でなく、「開」の状態をさらに複数の状態に切り換えることができるように構成されている。なお、比例電磁弁はラッチ式電磁弁と異なり、その状態保持のために通電が必要なため、基本的に商用電源に配線コードで接続されるようになっている。 Next, a third embodiment of the gas-liquid mixing apparatus and gas-liquid mixing system according to the present invention will be described.
The third embodiment differs from the second embodiment in that a proportional solenoid valve is used in place of the latch solenoid valve as the
例えば、前記実施形態では、本発明の気液混合装置2および気液混合システム1を、理美容目的として洗髪台に設けられるシャワーや家庭用の風呂場のシャワーなどに適用した例について説明したが、各種医療設備における医療用具等に適用してもよいのはもちろんである。また、家庭用の風呂や業務用の風呂に適用して、炭酸泉を製造する装置(システム)にも用いることができる。さらに、炭酸水を必要とする種々の装置(システム)にも適用することができる。 The technical scope of the present invention is not limited to the above embodiment, and various modifications can be made without departing from the spirit of the present invention.
For example, in the above-described embodiment, the gas-
原液中に気体を混合して気体混合液を製造する方法であって、
前記の気液混合装置を提供し、
前記原液を原液流入管に連続的に供給し、これと同時に前記気体を気体流入管に連続的に供給し、それにより、前記原液と前記気体とを対面して衝突させることによって混合し、
得られた原液と気体の混合物を、前記混合液配管に流入させる
ことを含む方法である。
本発明の方法に用いる気液混合装置、原液及び気体、並びに原液、気体を装置に供給する手順及び条件などについては、気液混合装置に関して前記した通りである。また、本発明の方法は、前記した本発明の気液混合システムを用いて実施することもできる。 Furthermore, in this invention, the method of mixing gas in a stock solution and manufacturing a gas liquid mixture is provided. That is, the method of the present invention comprises:
A method for producing a gas mixture by mixing a gas in a stock solution,
Providing the gas-liquid mixing device,
The stock solution is continuously supplied to the stock solution inflow pipe, and at the same time, the gas is continuously supplied to the gas inflow pipe, thereby mixing the stock solution and the gas by facing each other and mixing them,
It is a method including flowing the obtained mixture of undiluted solution and gas into the mixed solution pipe.
The gas-liquid mixing device, the raw solution and gas, the procedure and conditions for supplying the raw solution and gas to the device, etc. used in the method of the present invention are as described above for the gas-liquid mixing device. The method of the present invention can also be carried out using the gas-liquid mixing system of the present invention described above.
2 気液混合装置
3 原水供給源(原液供給源)
4 気体供給源
5 原水流入管(原液流入管)
6 気体流入管
7 気液衝突部
8 混合液配管
9 配管本体
10 ハウジング
11 案内管
12 内挿部
13 ハウジング本体
17 渦発生部材(渦発生部)
18 円筒部
18a テーパ面
19 偏流板
19a 案内口
20 溝部
21 大径部
21a 内部孔
21b テーパ面
22 小径部
22a 内部孔
23 ミキシングパイプ
24 溝部
25 狭隘部
26 流路変更部
27a 第1の邪魔板
27b 第2の邪魔板
27c 開口
32 第1の圧力スイッチ
33 電磁弁(制御弁)
36 パイプ
50 気液混合システム
52 制御弁
54 操作パネル
55 調整部 1 Gas-
4
6
18
36
Claims (15)
- 原液中に気体を混合して気体混合液を製造する気液混合装置であって、
前記原液が連続的に流入する原液流入管と、前記気体が連続的に流入する気体流入管と、前記原液流入管、前記気体流入管にそれぞれ連通する混合液配管とを備え、
前記原液流入管と前記気体流入管とが、前記原液と前記気体とが対面して衝突するように連通し、それにより、この連通箇所において、気液衝突部を形成し、
前記混合液配管を、前記気液衝突部に連通させるとともに、前記原液流入管の中心軸と前記気体流入管の中心軸のうち少なくとも一つを前記混合液配管の中心軸と異なる方向に配置した気液混合装置。 A gas-liquid mixing device for producing a gas mixture by mixing gas in a stock solution,
A stock solution inflow pipe through which the stock solution continuously flows, a gas inflow pipe through which the gas continuously flows, a mixture liquid pipe respectively connected to the stock solution inflow pipe and the gas inflow pipe,
The undiluted solution inflow pipe and the gas inflow tube communicate with each other so that the undiluted solution and the gas collide face each other, thereby forming a gas-liquid collision portion at this communicating location,
The mixed liquid pipe communicates with the gas-liquid collision portion, and at least one of the central axis of the raw liquid inlet pipe and the central axis of the gas inlet pipe is arranged in a direction different from the central axis of the mixed liquid pipe. Gas-liquid mixing device. - 前記原液流入管の中心軸と前記気体流入管の中心軸とのなす角度が20°~180°である請求項1記載の気液混合装置。 2. The gas-liquid mixing device according to claim 1, wherein an angle formed by a central axis of the stock solution inflow pipe and a central axis of the gas inflow pipe is 20 ° to 180 °.
- 前記原液が水であり、前記気体が炭酸ガスである請求項1又は2に記載の気液混合装置。 The gas-liquid mixing apparatus according to claim 1 or 2, wherein the stock solution is water and the gas is carbon dioxide gas.
- 前記混合液配管に、前記気体混合液に渦流を生じさせる、第1渦流生成機構が設けられている請求項1~3に記載の気液混合装置。 The gas-liquid mixing device according to any one of claims 1 to 3, wherein a first eddy current generating mechanism for generating a vortex in the gas liquid mixture is provided in the liquid mixture pipe.
- 前記第1渦流生成機構は、前記混合液配管内に設けられた環状または筒状の渦発生部の前記気液衝突部側の端部と、該端部に対向する前記混合液配管の内壁面との間において、前記気液衝突部側に開口して形成された溝部を備えている請求項4記載の気液混合装置。 The first vortex generating mechanism includes an end portion on the gas-liquid collision portion side of an annular or cylindrical vortex generating portion provided in the mixed solution pipe, and an inner wall surface of the mixed solution pipe facing the end portion. The gas-liquid mixing apparatus of Claim 4 provided with the groove part opened and formed in the said gas-liquid collision part side between.
- 前記第1渦流生成機構は、前記混合液配管の上流側に配設された上流側第1渦流生成機構と、該上流側第1渦流生成機構より下流側に配設された下流側第1渦流生成機構とを備えている請求項5記載の気液混合装置。 The first vortex generating mechanism includes an upstream first vortex generating mechanism disposed on the upstream side of the mixed solution pipe, and a downstream first vortex flow disposed on the downstream side of the upstream first vortex generating mechanism. The gas-liquid mixing apparatus of Claim 5 provided with the production | generation mechanism.
- 前記上流側第1渦流生成機構を構成する前記渦発生部の内部孔には、前記気体混合液を前記下流側第1渦流生成機構の前記内壁面側に案内する案内口が設けられている請求項6記載の気液混合装置。 A guide port that guides the gas mixture to the inner wall surface side of the downstream first vortex generating mechanism is provided in an internal hole of the vortex generating portion constituting the upstream first vortex generating mechanism. Item 7. The gas-liquid mixing device according to Item 6.
- 前記混合液配管には、該混合液配管を流れる気体混合液の流路を上流から下流に向けて狭めることにより、前記気体混合液に渦流を生じさせる、第2渦流生成機構が設けられている請求項1~7のいずれか一項に記載の気液混合装置。 The mixed liquid pipe is provided with a second eddy current generating mechanism for generating a vortex in the gas mixed liquid by narrowing a flow path of the gas mixed liquid flowing through the mixed liquid pipe from upstream to downstream. The gas-liquid mixing device according to any one of claims 1 to 7.
- 前記第2渦流生成機構は、前記混合液配管を流れる気体混合液の流路を上流から下流に向けて狭める狭隘部と、該狭隘部の側方に流路を変更することで前記気体混合液の流れを反転させ、渦流を生じさせる流路変更部と、を有して構成されている請求項8記載の気液混合装置。 The second eddy current generating mechanism includes a narrow portion that narrows a flow path of the gas mixture flowing through the mixed solution pipe from upstream to downstream, and a change of the flow path to the side of the narrow portion, thereby changing the gas mixture The gas-liquid mixing device according to claim 8, further comprising: a flow path changing unit that reverses the flow of the liquid and generates a vortex.
- 前記原液流入管には、該流路を流れる原液の圧力が所定の圧力以上になったことを検知する圧力スイッチが設けられ、
前記気体流入管には、該気体流入管と気体供給源との間に設けられて前記気体供給源から前記気体流入管への気体の供給を制御する制御弁が設けられ、
前記圧力スイッチは、原液の圧力が所定の圧力以上になったことを検知したら前記制御弁を開くように構成されている請求項1~9のいずれか一項に記載の気液混合装置。 The stock solution inflow pipe is provided with a pressure switch for detecting that the pressure of the stock solution flowing through the flow path is equal to or higher than a predetermined pressure,
The gas inflow pipe is provided with a control valve that is provided between the gas inflow pipe and the gas supply source and controls supply of gas from the gas supply source to the gas inflow pipe,
The gas-liquid mixing device according to any one of claims 1 to 9, wherein the pressure switch is configured to open the control valve when detecting that the pressure of the stock solution has become equal to or higher than a predetermined pressure. - 前記制御弁が、ラッチ式電磁弁によって構成されている請求項10記載の気液混合装置。 The gas-liquid mixing device according to claim 10, wherein the control valve is constituted by a latch type electromagnetic valve.
- 前記ラッチ式電磁弁は、電池で稼働する請求項11記載の気液混合装置。 The gas-liquid mixing device according to claim 11, wherein the latch type solenoid valve is operated by a battery.
- 前記制御弁が、比例電磁弁によって構成され、該比例電磁弁には、前記気体供給源から前記気体流入管への気体の供給量を調整する調整部が設けられている請求項10記載の気液混合装置。 11. The gas according to claim 10, wherein the control valve is constituted by a proportional solenoid valve, and the proportional solenoid valve is provided with an adjustment unit that adjusts a gas supply amount from the gas supply source to the gas inflow pipe. Liquid mixing device.
- 請求項1~13のいずれか一項に記載の気液混合装置と、
前記原液流入管に原液を供給する原液供給源と、
前記気体流入管に気体を供給する気体供給源と、
前記原液供給源からの前記原液流入管への原液の供給、および前記気体供給源からの前記気体流入管への気体の供給を制御する制御部と、を備える気液混合システム。 A gas-liquid mixing device according to any one of claims 1 to 13,
A stock solution supply source for supplying the stock solution to the stock solution inflow pipe;
A gas supply source for supplying gas to the gas inlet pipe;
A gas-liquid mixing system comprising: a control unit that controls supply of a stock solution from the stock solution supply source to the stock solution inflow tube and supply of gas from the gas supply source to the gas inflow tube. - 原液中に気体を混合して気体混合液を製造する方法であって、
請求項1~13のいずれか一項に記載の気液混合装置を提供し、
前記原液を原液流入管に連続的に供給し、これと同時に前記気体を気体流入管に連続的に供給し、それにより、前記原液と前記気体とを対面して衝突させることによって混合し、
得られた原液と気体の混合物を、前記混合液配管に流入させる
ことを含む方法。 A method for producing a gas mixture by mixing a gas in a stock solution,
A gas-liquid mixing device according to any one of claims 1 to 13 is provided,
The stock solution is continuously supplied to the stock solution inflow pipe, and at the same time, the gas is continuously supplied to the gas inflow pipe, thereby mixing the stock solution and the gas by facing each other and mixing them,
A method comprising flowing the obtained mixture of stock solution and gas into the mixed solution pipe.
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105708679A (en) * | 2016-01-26 | 2016-06-29 | 胥常委 | Carbonate spring preparation device and method |
WO2018023713A1 (en) * | 2016-08-05 | 2018-02-08 | Cornelius, Inc. | Apparatuses for mixing gases into liquids |
CN109966941A (en) * | 2019-05-13 | 2019-07-05 | 江苏炬焰智能科技有限公司 | Carbonate spring mixer |
US10477883B2 (en) | 2015-08-25 | 2019-11-19 | Cornelius, Inc. | Gas injection assemblies for batch beverages having spargers |
US10785996B2 (en) | 2015-08-25 | 2020-09-29 | Cornelius, Inc. | Apparatuses, systems, and methods for inline injection of gases into liquids |
US11040314B2 (en) | 2019-01-08 | 2021-06-22 | Marmon Foodservice Technologies, Inc. | Apparatuses, systems, and methods for injecting gasses into beverages |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IL248295B (en) | 2016-10-10 | 2018-02-28 | Strauss Water Ltd | Carbonation unit, system and method |
CN107261876B (en) * | 2017-07-31 | 2023-04-18 | 广东大任生物科技有限责任公司 | Gas-liquid mixing device |
US20200360875A1 (en) * | 2019-05-14 | 2020-11-19 | Sodastream Industries Ltd. | Carbonation machine and a gas canister for a carbonation machine |
CN111115787A (en) * | 2020-01-17 | 2020-05-08 | 南京昭凌精密机械有限公司 | Fusion device for preparing high-concentration carbonic acid spring |
TWI764774B (en) * | 2021-07-02 | 2022-05-11 | 信紘科技股份有限公司 | Gas-liquid mixing device and method |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001293342A (en) * | 2000-04-18 | 2001-10-23 | Mitsubishi Rayon Eng Co Ltd | Device and process for carbonated water |
JP2011240209A (en) * | 2010-05-14 | 2011-12-01 | Maindorei Gijutsu Kagaku Kenkyusho:Kk | Mechanism for generating microbubble |
JP2013529130A (en) * | 2010-05-03 | 2013-07-18 | アパイク インコーポレイテッド | Method of solubilizing carbon dioxide in water using high energy collisions |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3312354B2 (en) * | 1997-04-24 | 2002-08-05 | リンナイ株式会社 | Gas appliance equipped with a latch type solenoid valve |
JP3738440B2 (en) * | 2002-01-18 | 2006-01-25 | 株式会社ユアテック | Bubble generator |
JP2005118634A (en) * | 2003-10-14 | 2005-05-12 | Japan Science & Technology Agency | Micro-mixing device |
JP2008212495A (en) * | 2007-03-06 | 2008-09-18 | Hiroshi Sawakuri | Carbonated spring generator |
JP4964829B2 (en) * | 2008-06-09 | 2012-07-04 | 三菱レイヨン・クリンスイ株式会社 | Carbonated water production method and carbonated water production equipment |
US9144205B2 (en) * | 2008-10-17 | 2015-09-29 | Alchem Environmental Ip Llc | Hydroponics applications and ancillary modifications to a polyphasic pressurized homogenizer |
JP5894355B2 (en) | 2009-05-13 | 2016-03-30 | アムズ株式会社 | Gas mixed water generator |
DE102011083402A1 (en) * | 2011-09-26 | 2013-03-28 | Siemens Aktiengesellschaft | Mixing device for use in bioreactor for mixing carbon dioxide into suspension formed by nutrient solution for cultivation of e.g. algae, has diffuser for appeasing suspension such that gas in gas bubbles dissolves in suspension |
JP5243657B1 (en) * | 2012-12-19 | 2013-07-24 | 日科ミクロン株式会社 | Mixing device and installation structure of mixing device |
-
2015
- 2015-02-05 JP JP2015510207A patent/JP5952959B2/en not_active Expired - Fee Related
- 2015-02-05 TW TW104103881A patent/TWI584873B/en not_active IP Right Cessation
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- 2015-02-05 WO PCT/JP2015/053271 patent/WO2015119204A1/en active Application Filing
- 2015-02-05 TW TW105138831A patent/TWI615193B/en not_active IP Right Cessation
- 2015-02-05 KR KR1020167020740A patent/KR101858886B1/en active IP Right Grant
- 2015-02-05 TW TW105138873A patent/TWI629096B/en not_active IP Right Cessation
- 2015-10-13 JP JP2015202337A patent/JP6147313B2/en not_active Expired - Fee Related
- 2015-10-13 JP JP2015202336A patent/JP6224049B2/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001293342A (en) * | 2000-04-18 | 2001-10-23 | Mitsubishi Rayon Eng Co Ltd | Device and process for carbonated water |
JP2013529130A (en) * | 2010-05-03 | 2013-07-18 | アパイク インコーポレイテッド | Method of solubilizing carbon dioxide in water using high energy collisions |
JP2011240209A (en) * | 2010-05-14 | 2011-12-01 | Maindorei Gijutsu Kagaku Kenkyusho:Kk | Mechanism for generating microbubble |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US10477883B2 (en) | 2015-08-25 | 2019-11-19 | Cornelius, Inc. | Gas injection assemblies for batch beverages having spargers |
US10785996B2 (en) | 2015-08-25 | 2020-09-29 | Cornelius, Inc. | Apparatuses, systems, and methods for inline injection of gases into liquids |
US11013247B2 (en) | 2015-08-25 | 2021-05-25 | Marmon Foodservice Technologies, Inc. | Apparatuses, systems, and methods for inline injection of gases into liquids |
CN105708679A (en) * | 2016-01-26 | 2016-06-29 | 胥常委 | Carbonate spring preparation device and method |
WO2018023713A1 (en) * | 2016-08-05 | 2018-02-08 | Cornelius, Inc. | Apparatuses for mixing gases into liquids |
US11612864B2 (en) | 2016-08-05 | 2023-03-28 | Marmon Foodservice Technologies, Inc. | Apparatuses for mixing gases into liquids |
US11040314B2 (en) | 2019-01-08 | 2021-06-22 | Marmon Foodservice Technologies, Inc. | Apparatuses, systems, and methods for injecting gasses into beverages |
CN109966941A (en) * | 2019-05-13 | 2019-07-05 | 江苏炬焰智能科技有限公司 | Carbonate spring mixer |
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