CN211725361U

CN211725361U - Penetrating fluid concentration device for dynamic high-pressure micro-jet

Info

Publication number: CN211725361U
Application number: CN201922025369.9U
Authority: CN
Inventors: 杨雷
Original assignee: Nanchang University
Current assignee: Nanchang University
Priority date: 2019-11-21
Filing date: 2019-11-21
Publication date: 2020-10-23
Anticipated expiration: 2029-11-21

Abstract

The utility model discloses a developments high pressure is penetrant enrichment facility for microjet relates to the microjet field, for the not high problem of the current penetrant enrichment facility's among the solution prior art work efficiency. The improved reverse osmosis membrane comprises a connecting plate, a collecting plate, a reverse osmosis membrane, a liquid inlet nozzle, a collecting cylinder, a rotating plate, a fixing plate, a driving motor, a sealing plate, a liquid core column, a screen mesh, a hole, a through hole and a partition plate, wherein the collecting plate is installed below the connecting plate, the reverse osmosis membrane is installed at the upper end of the connecting plate, the liquid core column is installed inside the reverse osmosis membrane, the screen mesh is installed outside the liquid core column, the hole is formed in the inner surface of the liquid core column, the through hole is formed in the outer surface of the reverse osmosis membrane, the partition plate is installed inside the liquid storage tank, and a water pump is installed inside the partition plate.

Description

Penetrating fluid concentration device for dynamic high-pressure micro-jet

Technical Field

The utility model relates to a little efflux technical field specifically is a developments high pressure is penetrant enrichment facility for little efflux.

Background

The microfluid is under the pressure effect of the ultra-high pressure (310MPa), through the very tiny valve core of aperture, produce the fluid of several times of the speed of sound, thus reach and disperse, homogenize, emulsify, nanoparticle, etc., the microfluid is specified and does not need extra fluid source, the fluidic formation comes from the fluid around directly, this technology is proposed in the 70 s of 20 th century at the earliest, but get the full study until 90 s, the formation of microfluid mainly has two kinds of forms, one is that it forms the fluidic actuator to form by opening the closed cavity with the micropore on a side only, the opposite side of opening produces the vibration while working, the external fluid can enter, discharge the cavity through opening constantly, form the microfluid; the other is that the vibrating diaphragm is directly put into the environmental fluid, when the diaphragm vibrates, as long as the amplitude of the diaphragm is large enough, jet flow is formed along the normal direction of the diaphragm, and in the two forms, the generation of the vibration can be divided into an electromagnetic mechanical type, an electrostatic type and a piezoelectric type.

One of the application results of the micro-jet technology in aerodynamic control is that the lift-drag ratio of the model can be improved, the liquid used by the micro-jet needs to be processed by reverse osmosis, and the working efficiency of the existing penetrating fluid concentration device is not high; therefore, the market is urgently needed to develop a penetrating fluid concentration device for dynamic high-pressure micro-jet to help people to solve the existing problems.

SUMMERY OF THE UTILITY MODEL

An object of the utility model is to provide a developments high pressure is penetrant enrichment facility for microjet to solve the not high problem of the current penetrant enrichment facility's that provides work efficiency among the above-mentioned background art.

In order to achieve the above object, the utility model provides a following technical scheme: a penetrating fluid concentration device for dynamic high-pressure micro-jet flow comprises a concentration device shell, wherein a liquid inlet is installed on one side above the concentration device shell, an access panel is installed on the front end face below the concentration device shell, a liquid outlet pipe is installed on one side of the concentration device shell, a connecting pipe is installed on one side of the liquid outlet pipe, a liquid storage tank is installed on one side of the connecting pipe, a liquid outlet is arranged on the front end face of the liquid storage tank, a valve is installed at the upper end of the liquid outlet, a heater is installed on one side of the liquid storage tank, a connecting plate is installed above the interior of the concentration device shell, a collecting plate is installed below the connecting plate, a reverse osmosis membrane is installed below the collecting plate, a liquid inlet nozzle is arranged at the upper end of the reverse osmosis membrane, a, the improved reverse osmosis membrane comprises a rotating plate, and is characterized in that a fixing plate is installed below the inside of the rotating plate, a driving motor is installed below the fixing plate, an installation plate is installed at the upper end of the driving motor, a sealing plate is arranged at the upper end of the reverse osmosis membrane, a liquid permeating core column is installed inside the reverse osmosis membrane, a screen is installed outside the liquid permeating core column, a hole is formed in the inner surface of the liquid permeating core column, a through hole is formed in the outer surface of the reverse osmosis membrane, a partition plate is installed inside the liquid storage tank, and.

Preferably, the liquid inlet extends to the interior of the shell of the concentration device and is connected with the connecting plate in a sealing mode, a notch is formed in the lower portion of the connecting plate, and the bus board is rotatably connected with the notch through a bearing.

Preferably, the access panel passes through the set screw and is connected with the enrichment facility shell, drain pipe and enrichment facility shell welded connection, the drain pipe passes through flange and connecting pipe sealing connection.

Preferably, the liquid inlet nozzle is fixedly connected with the collecting plate, the reverse osmosis membrane extends to the inside of the fixing plate and is fixedly connected with the rotating plate, and the collecting cylinder is welded with the rotating plate.

Preferably, one end of the driving motor is connected with the shell of the concentration device through a fixing screw, and the other end of the driving motor penetrates through the mounting plate to be fixedly connected with the rotating plate through a coupler.

Preferably, the permeable liquid core column is hermetically connected with the reverse osmosis membrane through a sealing plate, the screen mesh is attached to the permeable liquid core column, the hole and the permeable liquid core column are integrated, and the through hole and the reverse osmosis membrane are integrated.

Compared with the prior art, the beneficial effects of the utility model are that:

1. the utility model discloses a through the setting of enrichment facility shell, before the use of microjet, earlier lead into the enrichment facility shell inside through the inlet, the fluid flows into reverse osmosis membrane inside through the cylinder manifold, filter reverse osmosis through permeate liquid stem and screen cloth inside reverse osmosis membrane, and in the filtering process, turn on driving motor, driving motor drives the rotor plate and rotates, drive reverse osmosis membrane through the rotor plate and rotate, through the centrifugal force that the rotation brought, throw away the internal fluid through hole and through-hole, thereby can improve filtration efficiency, have simple structure, good treatment effect, the investment running cost is low advantage, can make reverse osmosis membrane filter core replacement cycle effectively prolong, thereby save manpower, medicament and consumptive material by a wide margin, prolong reverse osmosis membrane life, increase the water yield, improve the fluid quality, thereby can concentrate the fluid according to the demand of microjet, is convenient and practical.

2. The utility model discloses a through the setting of liquid storage pot, the fluid after the concentration passes through inside the water pump inhales the liquid storage pot, through the connection of flange, can make things convenient for the connection between drain pipe and the connecting pipe and fix to conveniently operate, can conveniently control the temperature of the inside concentrate of liquid storage pot through the inside heater of liquid storage pot, thereby adapt to the service environment of microjet, the direct use of being convenient for improves the result of use.

Drawings

FIG. 1 is a front view of a dynamic high pressure micro-jet permeate concentrator of the present invention;

FIG. 2 is a cross-sectional view of the concentrator housing of the present invention;

FIG. 3 is a cross-sectional view of a reverse osmosis membrane of the present invention;

FIG. 4 is a view showing an internal structure of the liquid storage tank of the present invention.

In the figure: 1. a concentrator housing; 2. a liquid inlet; 3. an access panel; 4. a liquid outlet pipe; 5. a connecting pipe; 6. a liquid storage tank; 7. a liquid outlet; 8. a valve; 9. a heater; 10. a connecting plate; 11. a bus bar; 12. a reverse osmosis membrane; 13. a liquid inlet nozzle; 14. a collection cylinder; 15. a rotating plate; 16. a fixing plate; 17. a drive motor; 18. mounting a plate; 19. a sealing plate; 20. a liquid permeable wick; 21. screening a screen; 22. a hole; 23. a through hole; 24. a partition plate; 25. and (4) a water pump.

Detailed Description

The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments.

Referring to fig. 1-4, the present invention provides an embodiment: a penetrating fluid concentration device for dynamic high-pressure micro-jet comprises a concentration device shell 1, a liquid inlet 2 is installed on one side above the concentration device shell 1, an access panel 3 is installed on the front end face below the concentration device shell 1, a liquid outlet pipe 4 is installed on one side of the concentration device shell 1, a connecting pipe 5 is installed on one side of the liquid outlet pipe 4, a liquid storage tank 6 is installed on one side of the connecting pipe 5, a liquid outlet 7 is arranged on the front end face of the liquid storage tank 6, a valve 8 is installed at the upper end of the liquid outlet 7, a heater 9 is installed on one side of the liquid storage tank 6, a connecting plate 10 is installed above the interior of the concentration device shell 1, a confluence plate 11 is installed below the connecting plate 10, a reverse osmosis membrane 12 is installed below the confluence plate 11, a liquid inlet nozzle 13 is arranged at the upper end, a fixing plate 16 is installed below the inside of the rotating plate 15, a driving motor 17 is installed below the fixing plate 16, an installation plate 18 is installed at the upper end of the driving motor 17, a sealing plate 19 is arranged at the upper end of the reverse osmosis membrane 12, a permeable core column 20 is installed inside the reverse osmosis membrane 12, a screen 21 is installed outside the permeable core column 20, a hole 22 is formed in the inner surface of the permeable core column 20, a through hole 23 is formed in the outer surface of the reverse osmosis membrane 12, a partition plate 24 is installed inside the liquid storage tank 6, and a water pump 25 is installed inside the partition plate.

Further, inlet 2 extends to 1 inside and connecting plate 10 sealing connection of enrichment facility shell, and the below of connecting plate 10 is provided with the breach, and cylinder manifold 11 passes through the bearing to be connected with the breach rotation, and inside fluid passed through 2 leading-in enrichment facility shells 1 of inlet, fluid passed through cylinder manifold 11 and flowed into inside reverse osmosis membrane 12.

Further, access panel 3 is connected with enrichment facility shell 1 through the set screw, drain pipe 4 and 1 welded connection of enrichment facility shell, and drain pipe 4 passes through flange and 5 sealing connection of connecting pipe, through the connection of flange, can make things convenient for the connection between drain pipe 4 and the connecting pipe 5 and fix to conveniently operate.

Furthermore, the liquid inlet nozzle 13 is fixedly connected with the collecting plate 11, the reverse osmosis membrane 12 extends into the fixing plate 16 and is fixedly connected with the rotating plate 15, the collecting cylinder 14 is welded with the rotating plate 15, and fluid after the osmotic filtration is collected through the collecting cylinder 14 and can be discharged into the liquid outlet pipe 4.

Further, one end of a driving motor 17 is connected with the shell 1 of the concentration device through a fixing screw, the other end of the driving motor 17 penetrates through the mounting plate 18 to be fixedly connected with the rotating plate 15 through a coupler, the driving motor 17 drives the rotating plate 15 to rotate, and the rotating plate 15 drives the reverse osmosis membrane 12 to rotate.

Further, permeate through liquid stem 20 through closing plate 19 and reverse osmosis membrane 12 sealing connection, screen cloth 21 with permeate through liquid stem 20 laminating, hole 22 sets up structure as an organic whole with permeate through liquid stem 20, through-hole 23 sets up structure as an organic whole with reverse osmosis membrane 12, through rotating the centrifugal force that brings, throws away inside fluid through hole 22 and through-hole 23 to can improve filtration efficiency.

The working principle is as follows: when in use, before the micro jet is used, fluid is firstly led into the interior of the shell 1 of the concentration device through the liquid inlet 2, the fluid flows into the interior of the reverse osmosis membrane 12 through the confluence plate 11, the reverse osmosis is filtered through the permeable liquid core column 20 and the screen 21 in the interior of the reverse osmosis membrane 12, in the filtering process, the driving motor 17 is turned on, the driving motor 17 drives the rotating plate 15 to rotate, the reverse osmosis membrane 12 is driven to rotate through the rotating plate 15, the internal fluid is thrown out through the holes 22 and the through holes 23 by the centrifugal force caused by rotation, the fluid after the osmotic filtration is collected through the collection cylinder 14 and can be discharged into the liquid outlet pipe 4, the concentrated fluid is sucked into the interior of the liquid storage tank 6 through the water pump 25, the connection between the liquid outlet pipe 4 and the connecting pipe 5 can be convenient and fixed through the connection of the flange, thereby the operation is convenient, the temperature of the concentrated, thereby adapting to the use environment of the micro-jet and being convenient for direct use.

It is obvious to a person skilled in the art that the invention is not restricted to details of the above-described exemplary embodiments, but that it can be implemented in other specific forms without departing from the spirit or essential characteristics of the invention. The present embodiments are therefore to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.

Claims

1. A permeate concentration device for dynamic high-pressure micro-jets, comprising a concentration device housing (1), characterized in that: inlet (2) is installed to one side of enrichment facility shell (1) top, access panel (3) is installed to the preceding terminal surface of enrichment facility shell (1) below, drain pipe (4) is installed to one side of enrichment facility shell (1), connecting pipe (5) are installed to one side of drain pipe (4), liquid storage pot (6) is installed to one side of connecting pipe (5), the preceding terminal surface of liquid storage pot (6) is provided with liquid outlet (7), valve (8) are installed to the upper end of liquid outlet (7), heater (9) are installed to one side of liquid storage pot (6), connecting plate (10) are installed to the inside top of enrichment facility shell (1), cylinder manifold (11) is installed to the below of connecting plate (10), reverse osmosis membrane (12) are installed to the below of cylinder manifold (11), the upper end of reverse osmosis membrane (12) is provided with feed liquor mouth (13), a collecting cylinder (14) is arranged outside the reverse osmosis membrane (12), a rotating plate (15) is arranged at the lower end of the collecting cylinder (14), a fixed plate (16) is arranged below the inside of the rotating plate (15), a driving motor (17) is arranged below the fixed plate (16), an installation plate (18) is installed at the upper end of the driving motor (17), a sealing plate (19) is arranged at the upper end of the reverse osmosis membrane (12), a permeate liquid core column (20) is arranged inside the reverse osmosis membrane (12), a screen (21) is arranged outside the permeate liquid core column (20), the inner surface of the permeable liquid core column (20) is provided with a hole (22), the outer surface of the reverse osmosis membrane (12) is provided with a through hole (23), a partition plate (24) is installed inside the liquid storage tank (6), and a water pump (25) is installed inside the partition plate (24).

2. The apparatus according to claim 1, wherein the apparatus further comprises: the liquid inlet (2) extends to the interior of the shell (1) of the concentration device and is connected with the connecting plate (10) in a sealing mode, a notch is formed in the lower portion of the connecting plate (10), and the bus board (11) is connected with the notch in a rotating mode through a bearing.

3. The apparatus according to claim 1, wherein the apparatus further comprises: the access panel (3) is connected with the concentrator shell (1) through a fixed screw, the liquid outlet pipe (4) is connected with the concentrator shell (1) in a welding mode, and the liquid outlet pipe (4) is connected with the connecting pipe (5) in a sealing mode through a connecting flange.

4. The apparatus according to claim 1, wherein the apparatus further comprises: feed liquor mouth (13) and cylinder manifold (11) fixed connection, reverse osmosis membrane (12) extend to fixed plate (16) inside and rotor plate (15) fixed connection, a section of thick bamboo (14) and rotor plate (15) welded connection collect.

5. The apparatus according to claim 1, wherein the apparatus further comprises: one end of the driving motor (17) is connected with the shell (1) of the concentration device through a fixing screw, and the other end of the driving motor (17) penetrates through the mounting plate (18) to be fixedly connected with the rotating plate (15) through a coupler.

6. The apparatus according to claim 1, wherein the apparatus further comprises: permeate liquid stem (20) and reverse osmosis membrane (12) sealing connection through closing plate (19), screen cloth (21) and permeate liquid stem (20) laminating, hole (22) set up structure as an organic whole with permeate liquid stem (20), through-hole (23) set up structure as an organic whole with reverse osmosis membrane (12).