JP6339733B2 - Mixing unit, fluid mixing device, and mixed fluid generating device - Google Patents

Description

  The present invention relates to a mixing unit for mixing and processing a plurality of different fluids, a fluid mixing apparatus including the mixing unit, and a mixed fluid generating apparatus equipped with the fluid mixing apparatus. Examples of the plurality of different fluids include a combination of liquid and liquid, liquid and gas, and powder and liquid, which are finely and uniformly mixed.

  One form of the fluid mixing device is disclosed in Patent Document 1. That is, in Patent Document 1, a disk-shaped second diffusion element is disposed opposite to a disk-shaped first diffusion element in which a fluid inlet is formed at the center, and between the two diffusion elements. A diffusion / mixing unit that forms a diffusion / mixing channel that diffuses and mixes the fluid flowing in from the inlet on the center side in the radial direction toward the peripheral side, and a fluid outlet in the center The disc-shaped second collective element is arranged opposite to the disc-shaped first collective element, and the fluid flowing from the peripheral side between the two collective elements is radially directed toward the central portion side. Disclosed is a fluid mixing device that includes a collecting / mixing unit that forms a collecting / mixing channel that flows and collects and mixes, and that connects a terminal end of a diffusion / mixing channel and a starting end of the collecting / mixing channel Has been.

  The opposing surfaces of the first and second diffusing elements and the opposing surfaces of the first and second assembly elements are formed with a hexagonal recess group of appropriate identical depth and size in the honeycomb structure, and the opposing recesses Arrange them at different positions so that they communicate with each other, and in the diffusion / mixing flow path and the collecting / mixing flow path, the fluid flows in the radial direction while repeating the merging and splitting (dispersing) while meandering. ing.

JP-A-9-52034

  However, the fluid mixing device disclosed in Patent Document 1 includes a diffusion / mixing flow path that diffuses and mixes the fluid flowing in from the inflow port on the central portion side in the radial direction toward the peripheral portion, and the peripheral portion. Since the flow channel structure that gathers and mixes the fluid flowing in from the side in the radial direction toward the center is formed in the same way, it is more concentrated than the diffusion / mixing channel with high mixing and dispersion function.・ Although the number of dispersions in the mixing channel was much smaller, the pressure loss was the same as that in the diffusion / mixing channel. Therefore, it has been desired to reduce the power consumption of the pressurizing pump that pressurizes and supplies the fluid to the fluid mixing device, and to increase the flow rate (efficiency) of the processed fluid.

  Therefore, the present invention can reduce the pressure loss, reduce the power consumption of the pressurizing pump, and can increase the outflow amount (efficiency) of the mixed fluid. It is an object to provide a unit, a fluid mixing device, and a mixed fluid generating device.

In the mixing unit according to the present invention, the plate-like first element and the second element are arranged so that their surfaces are opposed to each other, and the gap between the start edges of both elements serves as an inflow port. Between the terminal edges of the elements is an outlet, and only one side of the first element and only one side of the second element facing the surface are formed with the recesses facing each other, and the recesses of the opposing recesses are Are arranged in different positions so as to communicate with each other, so that a plurality of different fluids to be mixed are introduced from the inflow port, and the inflowing fluid meanders from the inflow side to the outflow side. In addition , the width of the inflow port in the direction perpendicular to the fluid flow direction is wider than the width in the fluid flow direction.

  A fluid mixing apparatus according to the present invention includes a mixing unit according to claim 1 in a mixing case, and introduces a plurality of different fluids to be mixed into the mixing case, and introduces from the introducing port. And an outlet for deriving a mixed fluid in which a plurality of different fluids are mixed by the mixing unit. In the mixing case, a plurality of mixing units can be arranged along the flow path and arranged in series at intervals. A plurality of the mixing units can be superposed in a stacked manner to form a mixed unit laminate.

  The mixed fluid generation device according to the present invention includes the fluid mixing device, a liquid as the fluid, and a means for introducing the liquid, gas, or powder as the fluid into the fluid mixing device. And liquid, liquid and gas, or liquid and powder are mixed.

  According to the present invention, the following effects are produced. That is, in the present invention, since pressure loss can be reduced, it is possible to reduce the power consumption of the mixing unit, the fluid mixing device, and the pressurizing pump that pressurizes and supplies the fluid to the mixed fluid generating device. In addition, it is possible to increase (efficiency) the outflow amount (derived amount) of the mixed processed fluid.

BRIEF DESCRIPTION OF THE DRAWINGS The conceptual explanatory drawing of the mixed fluid production | generation apparatus which comprises the fluid mixing apparatus which concerns on this invention. The perspective explanatory view of a fluid mixing device. II sectional view explanatory drawing of FIG. II-II sectional view explanatory drawing of FIG. Expansive plane explanatory drawing (a) and a cross-sectional enlarged side explanatory drawing (b) of a mixing unit. The table | surface which shows the time-dependent measurement result of DO value.

  Hereinafter, a fluid mixing apparatus according to the present invention will be described with reference to the drawings. Before that, a mixed fluid generating apparatus including the fluid mixing apparatus will be described with reference to the drawings.

[Description of mixed fluid generator]
A shown in FIG. 1 is a mixed fluid generating device that generates a mixed fluid, and the mixed fluid generating device A includes a fluid mixing device M according to the present invention. In the present embodiment, a treated liquid W such as water or seawater is used as a fluid as a continuous phase, and a gas-liquid mixed fluid using a gas such as air, oxygen gas, or nitrogen gas as a fluid as a dispersed phase is generated. Will be described. That is, the mixed fluid generating apparatus A connects the base end of the circulation pipe J to the bottom of the top-opening box-shaped tank T containing the treated water W, and the distal end of the circulation pipe J is connected to the treated water W in the tank T. By inserting it inside, the circulation flow path Cy for circulating the fluid in the tank T and the circulation pipe J is formed. A gas supply part K2 is connected to the middle part of the circulation pipe J via a gas supply pipe K1, and a fluid mixing device M is connected to the downstream side of the gas supply part K2. The fluid mixing device M mixes the gas with the treated water W by applying shearing force to the gas-liquid mixed phase of the gas supplied from the gas supply unit K2 and the treated water W to form a group of bubbles having ultrafine bubbles. It is configured to do.

  A suction pump Pa and a discharge pump Pb are arranged adjacent to each other in the middle of the circulation pipe J located on the downstream side of the tank T in series. Then, a gas supply part K2 is connected to a part of the circulation pipe J located between the discharge port of the suction pump Pa arranged on the upstream side and the suction port of the discharge pump Pb arranged on the downstream side via the gas supply pipe K1. doing. Here, the discharge pressure of the suction pump Pa is set to be equal to or lower than the suction pressure of the discharge pump Pb. V1 is a gas supply amount adjustment valve provided in the middle of the gas supply pipe K1, V2 is a pressure adjustment valve attached to the tip of the circulation pipe J, and Wk can supply treated water W as a solvent into the tank T at any time. The treated water supply unit.

  A backwash channel Bw is connected in communication with the circulation channel Cy described above. That is, one end of the backwash bypass pipe U is connected to the portion of the circulation pipe J located immediately upstream of the fluid mixing apparatus M via the upstream three-way valve V3. One end portion of the backwash bypass pipe U is connected to the circulation pipe J located on the immediately downstream side via the downstream three-way valve V4. A midway three-way valve V5 is provided in the middle of the backwash detour pipe U, and the drainage accommodating portion H is connected via the midway three-way valve V5. The backwash flow path Bw is formed by communicating the circulation pipe J and the backwash bypass pipe U via the upstream / downstream three-way valves V3 and V4. Then, the wash water stored in the tank T is circulated by the suction pump Pa and / or the discharge pump Pb in the backwash flow path Bw a required number of times, so that the wash water is supplied from the downstream side to the upstream side of the fluid mixing device M. The inside of the fluid mixing device M can be washed (backwashed) by flowing backward. After the back washing treatment, the washing waste water can be discharged to the waste water storage portion H through the midway three-way valve V5 provided in the middle of the backwash bypass pipe U. Thereafter, the circulation channel Cy is restored by restoring the three-way valves V3, V4, V5, and the fluid mixing process can be resumed by accommodating the treated water W in the tank T.

  In the mixed fluid generating apparatus A configured as described above, the gas supplied from the gas supply unit K2 disposed between the suction pump Pa and the discharge pump Pb is allowed to cooperate with the discharge port of the suction pump Pa. The suction pressure from the suction port of the discharge pump Pb and the suction pressure (ejector effect) are received smoothly and stably. As a result, a constant amount of gas mixed into the treated water W can be secured. Moreover, in this embodiment, since the suction pump Pa and discharge pump Pb with small power consumption can be used in cooperation, ensuring the production capability of the mixed fluid of the treated water W and the gas, the mixed fluid generator A Manufacturing costs and running costs can be reduced.

  For example, by performing a treatment operation for circulating the treated water W and nitrogen gas in the circulation flow path Cy for a predetermined number of circulations or for a predetermined time, oxygen dissolved in the treated water W is released and nitrogen gas is treated with the treated water W. The treated water W can be made into nitrogen water by being dissolved therein. According to the mixed fluid generating apparatus A, for example, the DO value (dissolved oxygen amount) of the 1t treated water W can be reduced to 1 mg / L or less within 60 minutes (see FIG. 6).

  Further, by operating the upstream / downstream three-way valves V3 and V4 to form the backwash flow path Bw, the washing water is caused to flow backward from the downstream side of the fluid mixing device M to wash the inside of the fluid mixing device M. (Backwashing) can be processed. After the back washing process, the washing waste water can be discharged to the waste water storage portion H through the midway three-way valve V5. Thereafter, the fluid mixing process can be easily restarted by restoring the three-way valves V3, V4, and V5. Thus, the fluid mixing function of the fluid mixing device M can be ensured satisfactorily by appropriately performing the backwash process.

[Description of fluid mixing device]
The fluid mixing apparatus M will be described with reference to FIGS. As shown in FIGS. 2 to 5, the fluid mixing device M is provided with an introduction port 11 for introducing a plurality of different fluids (treated water W and gas in this embodiment) R to be mixed in a pressurized state. A plurality of mixing units 20 that mix the fluid R introduced from the introduction port 11 are disposed in the mixing case 10, and the mixing case 10 is mixed fluid Rm (processed in this embodiment) mixed by the mixing unit 20. A lead-out port 12 for leading out water W and a gas-liquid mixed gas) is provided.

  In the mixing case 10, a plurality of mixing units 20 are arranged in series at intervals from the introduction port 11 side to the outlet port 12 side to form a relay reservoir space Sh between the mixing units 20. At the same time, an inlet side reservoir space Su is formed between the inlet port 11 and the mixing unit 20 arranged on the most upstream side, while an outlet port is provided between the mixing unit 20 arranged on the most downstream side and the outlet port 12. A side reservoir space Sd is formed, and the mixing unit 20 is arranged in communication between the reservoir spaces Su, Sh, Sd.

  The mixing unit 20 is configured such that the surfaces of the plate-like first element 30 and the second element 40 are arranged so as to face each other, and the gap between the start edge portions of both the elements 30, 40 serves as the inlet 50. 40 is formed as an outlet 51, and a plurality of recess groups 32, 42 having the same depth and size are formed on the opposing surfaces 31, 41 of both elements 30, 40 from the inlet 50 side. 51. The concave portions 34 and 44 facing each other are arranged at different positions so as to communicate with each other, and the concave portions 34 and The fluid R is configured so as to flow from the inlet 50 side toward the outlet 51 side while repeating the merging and splitting while meandering between the fluids 44.

  The fluid mixing device M of this embodiment forms a mixing unit stack 60 by superposing and arranging a plurality (10 in this embodiment) of the mixing units 20 in a stacked manner, and introducing the mixing unit 10 into the inlet port in the mixing case 10. 11 and the outlet 12, between the inlet-side reservoir space Su and the relay reservoir space Sh, between the relay reservoir space Sh and the relay reservoir space Sh, and between the relay reservoir space Sh and the outlet-side reservoir space Sh. A mixed unit laminate 60 is disposed between each Sd. In other words, in the present embodiment, a plurality (four in the present embodiment) of the mixing unit stacks 60 are arranged in series in the mixing case 10 with a certain interval from the upstream side toward the downstream side. . The inflow port 50 of each mixing unit 20 is arranged to open toward the inlet 11 side, while the outflow port 51 of each mixing unit 20 is arranged to open toward the outlet 12 side.

  In the fluid mixing apparatus configured as described above, the following operational effects are produced. That is, between the inlet 11 and the outlet 12 in the mixing case 10, between the inlet-side reservoir space Su and the relay reservoir space Sh, between the relay reservoir space Sh and the relay reservoir space Sh, and between the relay Since the mixing units 20 are arranged so as to communicate with each other between the reservoir space Sh and the outlet-side reservoir space Sd, the fluid R flowing in the mixing case 10 flows into each of the reservoir spaces Su, Sh, A pulsating flow is steadily caused by passing through Sd and each mixing unit 20 which becomes flow resistance alternately in series.

  That is, although the flow rate of the fluid R flowing in the pool spaces Su, Sh, Sd having almost no flow resistance is relatively large, the fluid R flowing in each mixing unit 20 having a mixing function receives the flow resistance and receives the flow resistance. The flow rate is relatively reduced. Therefore, the flow velocity of the fluid R flowing in the mixing case 10 is changed (absolutely changed) from large → small → large → small → large, and the flow of the fluid R becomes a steady pulsating flow. As a result, not only when flowing in each mixing unit 20, but also when flowing as a pulsating flow in the mixing case 10, a shearing effect is generated and a synergistic shearing effect is obtained.

  Further, the reservoir spaces Su, Sh, Sd are respectively arranged on the upstream side and the downstream side of each mixing unit 20, and the inflow port 50 of each mixing unit 20 is opened toward the introduction port 11 side. Since the outlet 51 of the mixing unit 20 is arranged to open toward the outlet 12, pressure loss in the mixing case 10 can be reduced. Therefore, the power consumption of the suction pump Pa and the discharge pump Pb that pressurizes and supplies the fluid to the fluid mixing device M can be reduced, and the outflow amount (derived amount) of the mixed fluid Rm that is the mixed fluid Increase (efficiency) can be achieved.

  In the present embodiment, the fluid R is introduced into the mixing case 10 in a pressurized state through the inlet 11 by the suction pump Pa and the discharge pump Pb, and the fluid R is mixed by the mixing unit 20 disposed in the mixing case 10. Thus, the mixed fluid Rm that has been mixed can be led out of the mixing case 10 from the outlet 12.

  In the mixing unit 20, the fluid R is caused to flow in from the inlet 50 between the starting edge portions of the plate-like first element 30 and the second element 40 whose surfaces are arranged to face each other. Until the fluid R flows out from the outlet 51 which is between the end edges of each of the recesses, the fluid R is caused to meander and flow between the concavities 34 and 44 opposed to each other in the concave groups 32 and 42 while repeating merging and splitting. Thus, the mixed fluid Rm can be generated steadily.

  At this time, a fluid (dispersed gas in this embodiment) is formed by a shearing force received when the fluid R composed of the continuous phase and the dispersed phase flows while meandering between the recesses 32 and 42 on the inlet side (upstream side). ) Is refined to produce a mixed fluid Rm.

  As described above, in the continuous flow path from the inlet 50 to the outlet 51 while repeating the merging and branching while the fluid R meanders between the opposing recesses 34 and 44 of the respective recess groups 32 and 42, as a dispersed phase. Since the fluid is refined a plurality of times while receiving different shearing forces, it is possible to steadily and efficiently perform micronization or nanoscale refinement generation.

  In the fluid mixing apparatus M of the present embodiment, a plurality of mixing unit laminates 60 formed by superposing and arranging the mixing units 20 in a stacked manner are disposed in the mixing case 10, and therefore these mixing unit laminates 60 can generate a large amount of the mixed fluid Rm. Therefore, the generation efficiency of the mixed fluid Rm can be increased. As a result, the fluid mixing device M can generate the mixed fluid Rm with high mixing accuracy (for example, fineness and uniformity) just by passing the fluid R once (one pass), and passes the fluid R a predetermined number of times. By doing so, a desired mixed fluid Rm can be obtained in a short time.

  Next, the configuration of the fluid mixing device M will be described more specifically. That is, the mixing case 10 is formed in a rectangular box shape extending in one direction (left and right direction in the present embodiment), and has a rectangular plate-like ceiling portion 13 and bottom portion 14 extending in the left and right direction, and the ceiling portion 13 and A rectangular plate-shaped front, rear, left and right side wall portions 15, 16, 17, 18 interposed between front, rear, left and right side edges of the bottom portion 14 are formed. A circular inlet 11 is provided at the center of the right side wall 18, and the upstream end of the middle part of the circulation pipe J is connected to the inlet 11, and fluid R is added from the inlet 11 through the circulation pipe J. Introduced under pressure. A circular outlet 12 having a diameter smaller than that of the inlet 11 is provided at the center of the left side wall 17, and the downstream end of the middle portion of the circulation pipe J is connected to the outlet 12 to be mixed by the mixing unit 20. The mixed fluid Rm thus led out is led out from the outlet 12 through the circulation pipe J.

  The concave group 32 of the mixing unit 20 has a regular hexagonal opening shape (bottom view) and a bottomed cylindrical concave portion 34 extending in the extending direction (in this embodiment, with no gap) in the width direction (front-rear direction in this embodiment). A plurality of rows (4 rows in the present embodiment) are arranged adjacent to each other in the left-right direction, and the recesses 34 are opened downward. A large number of recesses 34 are formed in a so-called honeycomb shape.

  Further, the concave group 42 of the mixing unit 20 has a regular hexagonal bottomed cylindrical concave portion 44 on the side of the inflow port 50 of the opposing surface 41 of the second element 40 with a gap across the width direction (the front-rear direction in this embodiment). In a state where there is no protrusion, a plurality of rows (four rows in this embodiment) are provided adjacent to each other in the extending direction (left and right in this embodiment), and the recess 44 is opened upward. A large number of recesses 44 are formed in a so-called honeycomb shape.

  The recesses 34 that form the recess group 32 and the recesses 44 that form the recess group 42 are arranged opposite to each other and arranged at different positions so as to communicate with each other. That is, the corner 46 (36) of the recess 44 (34) is in contact with the center position of the recess 34 (44). Therefore, for example, when the case where the fluid R flows from the concave portion 34 side of the first element 30 to the concave portion 44 side of the second element 40 is considered, the fluid R is divided (distributed) into two flow paths. That is, the corner portion 46 of the second element 40 located at the center position of the recess 34 of the first element 30 functions as a flow dividing portion for dividing the fluid R. On the contrary, when the case where the fluid R flows from the second element 40 side to the first element 30 side is considered, the fluid R flowing from the two directions flows into one concave portion 34 to be joined. In this case, the corner portion 36 of the first element 30 positioned at the center position of the recess 44 of the second element 40 functions as a merging portion.

  The mixing unit 20 may be configured integrally by forming each part (constituent member) with a synthetic resin such as an acrylic resin and bonding them together with an adhesive, or an alloy such as stainless steel. Each part can be formed by the above, and these can be integrally assembled by screwing together.

  In the present embodiment, the flow width of the fluid R is the inflow / outflow width of the fluid R rather than the lateral width W2 of the mixing unit 20 (the width in the flow direction of the fluid R flowing from the inlet to the outlet). The mixing unit 20 is formed in a strip shape having a wide front and rear width W5 (width in a direction substantially perpendicular to the flow direction of the fluid R and the same width as the distance between the front and rear wall portions 15 and 16). The left-right width W1 of the inlet-side reservoir space Su is substantially the same width as the left-right width W2 of the mixing unit 20, and the left-right width W3 of the relay reservoir space Sh is substantially half the left-right width W2 of the mixing unit 20. The left-right width W4 of the outlet-side pool space Sd is substantially the same width as the left-right width W2 of the mixing unit 20. The front-rear width and the vertical width of each pool space Su, Sh, Sd are the same as the front-rear width and the vertical width of the inner surface of the mixing case 10. Then, the downstream side surface of the inlet-side reservoir space Su and the respective inlets 50 of the first mixing unit stacked body 60 arranged on the most upstream side are in surface contact and communicate with each other. The outlet 51 and the upstream side surface of the first relay pool space Sh formed on the uppermost stream side are in surface contact and communicate with each other, and the downstream side surface of the first relay pool space Sh and each of the second mixing unit stack 60 The inflow port 50 communicates in surface contact with each other, and each outflow port 51 of the second mixing unit stack 60 communicates with the upstream side surface of the second relay reservoir space Sh in surface contact with each other, so that the second relay reservoir. The downstream side surface of the space Sh and each inflow port 50 of the third mixing unit stack 60 are in surface contact and communicate with each other, and each outflow port 51 of the third mixing unit stack 60 and the third relay reservoir space Sh are connected. The upstream side surface communicates with and communicates with the downstream side surface of the third relay reservoir space Sh. The inflow ports 50 of the mixing unit laminate 60 are in surface contact with each other, and the outflow ports 51 of the fourth mixing unit laminate 60 are in surface contact with the upstream side surface of the outlet side reservoir space Sd to communicate with each other. doing.

  In this way, the fluid R introduced from the inlet 11 and filling the inlet-side reservoir space Su flows in parallel from the respective inlets 50 of the first mixing unit stack 60 into the respective mixing units 20. Then, by flowing while repeating the merging and splitting (dispersing) while meandering in each mixing unit 20, the mixed fluid Rm is refined and uniformly mixed with the gas as the dispersed phase under shearing force. Become.

  Subsequently, the mixed fluid Rm flows out from each outlet 51 of each mixing unit 20 of the first mixing unit stack 60 and fills the first relay pool space Sh. The mixed fluid Rm filled in the first relay reservoir space Sh flows in parallel into each mixing unit 20 from each inflow port 50 of the second mixing unit stack 60, and in each mixing unit 20, The mixing process is performed in the same manner as the mixing unit laminate 60 of one. As a result, the gas that is the dispersed phase is further refined and the mixed fluid Rm is uniformly mixed.

  Subsequently, the mixed fluid Rm flows out from each outflow port 51 of each mixing unit 20 of the second mixing unit stack 60 and fills the second relay reservoir space Sh. The mixed fluid Rm filled in the second relay reservoir space Sh flows in parallel from the respective inlets 50 of the third mixing unit stack 60 into the respective mixing units 20, where The mixing process is performed in the same manner as the mixing unit laminate 60 of No. 2. As a result, the gas that is the dispersed phase is further refined and the mixed fluid Rm is uniformly mixed.

  Subsequently, the mixed fluid Rm flows out from each outflow port 51 of each mixing unit 20 of the third mixing unit stack 60 and fills the third relay pool space Sh. The mixed fluid Rm filled in the third relay reservoir space Sh flows in parallel into each mixing unit 20 from each inflow port 50 of the fourth mixing unit stack 60, and in each mixing unit 20, The mixing process is performed in the same manner as the mixing unit laminate 60 of No. 3. As a result, the gas that is the dispersed phase is further refined and the mixed fluid Rm is uniformly mixed.

  Subsequently, the mixed fluid Rm flows out from the outlets 51 of the mixing units 20 of the fourth mixing unit stack 60 and fills the outlet-side pool space Sd. The mixed fluid Rm filled in the outlet port side reservoir space Sd is led out from the outlet port 12.

  In each mixing unit 20, the front-rear width W5 of each mixing unit 20 that is the inflow / outflow width of the fluid R is formed wider than the left-right width of each mixing unit 20 that is the flow width of the fluid R. Fluid R flows through each mixing unit 20 in a short time.

  Thus, in the mixing case 10, the fluid R or the mixed fluid Rm is introduced into the inlet 11 → the inlet-side reservoir space Su → the first mixing unit laminate 60 → the first relay reservoir space Sh → the second mixing unit. Stack 60 → second relay pool space Sh → third mixing unit stack 60 → third relay pool space Sh → fourth mixing unit stack 60 → outlet side reservoir space Sd → outlet 12 and flow To do.

  At this time, in the mixing case 10, the pool spaces Su, Sh, Sd having a relatively small channel resistance and the first to fourth mixing unit laminates 60 having a relatively large channel resistance are alternately arranged. Therefore, the fluid R flowing in the mixing case 10 or the pulsating flow in which the flow velocity of the mixed fluid Rm changes suddenly and suddenly can be obtained. Therefore, the fluid R receives the shearing force when flowing in the mixing case 10 as well as the shearing force when flowing in each mixing unit 20 as well as the pulsating flow in the mixing case 10. As a result, the shear effect acting on the fluid R can be increased, the dispersed phase can be refined to the nano level (1 μm or less), and a large amount of the mixed fluid Rm can be generated.

  In the present embodiment, the mixing unit stack 60 can be formed in a compact manner by arranging the required number (10) of the mixing units 20 in the mixing case 10 in a stacked manner. By disposing (four) mixing unit stacks 60 at intervals from the upstream side to the downstream side, the fluid mixing processes by the mixing units 20 can be performed simultaneously and efficiently. Therefore, an appropriate amount of the mixed fluid Rm can be efficiently generated by the appropriate number of the mixing units 20 disposed in a compact manner in the mixing case 10 and can be derived from the mixing case 10.

  The fluid mixing device M configured as described above connects the introduction port 11 to the discharge portion of the submersible pump, and discharges a plurality of different fluids sucked from the suction portion of the submersible pump into the fluid mixing device M from the discharge portion. The fluid mixing process can also be performed by causing the fluid mixing apparatus M to flow.

  An experiment was performed in which a gas-liquid mixed fluid was generated by the mixed fluid generating apparatus A including the fluid mixing apparatus M described above. That is, seawater was adopted as a fluid as a continuous phase, and nitrogen gas was adopted as a fluid as a dispersed phase. Seawater having a salt concentration of 3.4% was accommodated in the tank T, and the seawater was circulated through the circulation pipe J, and nitrogen was supplied from the gas supply unit K2 at 3.0 L / min. At this time, the discharge amount from the discharge pump Pb, which is a land pump (output: 2.2 kW) manufactured by Tsurumi Manufacturing Co., Ltd., was 260.0 L. In this experiment, the suction pump Pa was not used.

  The DO value (Dissolved Oxygen) which is the amount of dissolved oxygen in the produced gas-liquid mixed fluid (nitrogen seawater) was measured. The results are as shown in FIG. 6 (a table showing the results of measurement of DO values over time), whereas the DO value at the start of the experiment was 7.24 mg / L, whereas it was 0 after mixing for 1 hour. It was drastically reduced to .17 mg / L.

  Then, the total number of bubbles such as nitrogen of 1 μm or less (nano level) was measured with a nanoparticle analyzer “NanoSight NS500” manufactured by Nanosite. As a result, the density of nanobubbles in raw seawater was 0.992 billion / ml, whereas the density of nanobubbles after 1 hour mixing was 230 billion / ml, doubling 2.5 times. It was.

  In the above-described experiment, it was confirmed that the DO value can be efficiently reduced and the nanobubble density can be doubled by generating the gas-liquid mixed fluid by the mixed fluid generating apparatus A including the fluid mixing apparatus M. As a result, it was found that the fluid mixing apparatus M has good fluid shear efficiency and finer efficiency.

A Mixed fluid generation device M Fluid mixing device Cy Circulation flow path J Circulation pipe K1 Gas supply pipe K2 Gas supply section R Fluid Rm Mixed fluid W Processed water 10 Mixing case 11 Inlet 12 Outlet 20 Mixing unit 30 First element 40 First 2 elements 50 inlet 51 outlet

Claims (5)

The plate-like first element and the second element are arranged so that their faces are opposed to each other, and the flow between the end edges of both elements is provided between the start edges of both elements. Without exit,
The concave portions are formed to face each other only on one side of the first element and only on one side of the second element facing the surface, and the concave portions of the opposing concave groups are arranged in different positions so as to communicate with each other. by arranging a plurality of different fluids are mixed processed from the inlet by the inflow, constructed as flowed fluid is mixed by flowing toward the outlet side from the inlet side while meandering ,
Moreover , the mixing unit is formed so that the width of the inlet in the direction orthogonal to the fluid flow direction is wider than the width in the fluid flow direction. In a mixing case, the mixing unit according to claim 1 is arranged,
A fluid in which a mixing case is provided with an introduction port for introducing a plurality of different fluids to be mixed and a lead-out port for deriving a mixed fluid in which a plurality of different fluids introduced from the introduction port are mixed by a mixing unit Mixing equipment.   The fluid mixing apparatus according to claim 2, wherein a plurality of mixing units are arranged along the flow path and arranged in series at intervals in the mixing case.   The fluid mixing device according to claim 2 or 3, wherein a plurality of mixing units are arranged in a stacked manner to form a mixing unit laminate. The fluid mixing device according to any one of claims 2 to 4,
Means for introducing liquid as fluid and liquid, gas or powder as fluid into the fluid mixing device;
A mixed fluid generating apparatus configured to mix liquid and liquid, liquid and gas, or liquid and powder.

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