CN215975380U - Mineral spring nanofiltration ultrafiltration liquid concentration extraction equipment - Google Patents
Mineral spring nanofiltration ultrafiltration liquid concentration extraction equipment Download PDFInfo
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- CN215975380U CN215975380U CN202122093945.0U CN202122093945U CN215975380U CN 215975380 U CN215975380 U CN 215975380U CN 202122093945 U CN202122093945 U CN 202122093945U CN 215975380 U CN215975380 U CN 215975380U
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Abstract
The utility model discloses mineral spring nanofiltration ultrafiltration liquid concentration and extraction equipment which comprises a bottom plate, wherein a seat box is fixedly connected to the upper surface of the bottom plate, a heating box is arranged inside the seat box, a treatment box is fixedly connected to the upper surface of the heating box, a guide pipe is arranged inside the treatment box, one end of the guide pipe extends into the heating box, transverse plates are fixedly connected to the side surfaces of the guide pipe, leakage nets are fixedly connected to the side surfaces of the transverse plates, one ends, far away from the transverse plates, of the leakage nets are fixedly connected with the inner walls of the two sides of the treatment box, an extraction box is arranged inside the treatment box, the upper surface of the extraction box is fixedly connected with the lower surfaces of the leakage nets, a return pipe is fixedly connected to the lower surface of the extraction box, a cooling box is arranged inside the seat box, and the cooling box is positioned on the left side of the heating box. The mineral spring temperature-reducing device can quickly reduce the temperature of concentrated and extracted mineral spring through the installed device in the using process.
Description
Technical Field
The utility model relates to the field of nanofiltration ultrafiltration, in particular to mineral spring nanofiltration ultrafiltration liquid concentration and extraction equipment.
Background
The ultrafiltration technology is a membrane separation process which takes screening as a separation principle and pressure as a driving force, can effectively remove particles, colloid, bacteria, high-molecular organic matters and the like in water, can be widely applied to separation, concentration and purification of substances, has no phase transformation in the ultrafiltration process, and has good temperature resistance, acid and alkali resistance and oxidation resistance, the ultrafiltration membrane adopts different construction forms, membrane materials and process design, and can adapt to various water quality conditions and separation functions, nanofiltration is a pressure-driven membrane separation process between reverse osmosis and ultrafiltration, the pore diameter range of the nanofiltration membrane is about a few nanometers, the occurrence of the nanofiltration membrane is late compared with other pressure-driven membrane separation processes, the occurrence of the nanofiltration membrane can be traced to the end of the 70 years, the nanofiltration is developed rapidly, and the membrane module is commercialized in the middle of the 80 years.
1. After the stock solution is boiled and vaporized, the vaporized stock solution is collected and intensively discharged into a concentration and extraction device, so that liquefaction reflux is easy to occur to cause waste.
2. After the raw liquid is concentrated and extracted, the raw liquid is usually kept stand for cooling, so that the efficiency is relatively low, and the extraction efficiency is easily influenced.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the defects in the prior art and provides mineral spring nanofiltration ultrafiltration liquid concentration and extraction equipment.
In order to achieve the purpose, the utility model adopts the following technical scheme: the utility model provides a mineral spring is received and is strained concentrated extraction equipment of ultrafiltration liquid, includes the bottom plate, the last fixed surface of bottom plate is connected with the seat case, the inside of seat case is provided with the heating cabinet, the last fixed surface of heating cabinet is connected with handles the case, the inside of handling the case is provided with the pipe, and the one end of pipe extends into the inside of heating cabinet.
The side surface of pipe fixedly connected with diaphragm, the equal fixedly connected with of side surface of diaphragm leaks the net, and leaks the net and keep away from the one end of diaphragm and the both sides inner wall fixed connection who handles the case.
The inside of handling the case is provided with draws the box, and draws the upper surface of box and the lower fixed surface who leaks the net and be connected, the lower fixed surface who draws the box is connected with the back flow.
The inside of seat case is provided with the cooling box, and the cooling box is located the left side of heating cabinet, the one end that the case was kept away from to the back flow extends into the inside of cooling box, the last fixed surface of cooling box is connected with the motor.
The output fixedly connected with bull stick of motor, and the bull stick is located the inside of cooling box, the side surface evenly distributed of bull stick has the stirring leaf, the front surface of stirring leaf is equipped with the recess.
As a further description of the above technical solution:
the rear surface of the cooling box is fixedly connected with a refrigerating plate, the left side surface of the cooling box is fixedly connected with a liquid discharge valve, the front surface of the processing box is fixedly connected with a temperature sensor, and an electric heating tube is arranged in the heating box.
As a further description of the above technical solution:
the upper surface of bottom plate passes through support column fixedly connected with ultrafiltration jar, ultrafiltration jar's inside is provided with the milipore filter, ultrafiltration jar's front surface fixedly connected with barometer.
As a further description of the above technical solution:
the last fixed surface of ultra-filtration jar is connected with discharge valve, the last fixed surface of ultra-filtration jar is connected with feed liquor pipe one, and feed liquor pipe one is located discharge valve's left side, the side surface fixedly connected with booster pump of feed liquor pipe one.
As a further description of the above technical solution:
the upper surface of the base plate is fixedly connected with a first water pump, the first water pump is located on the left side of the ultrafiltration tank, the first input end of the first water pump is fixedly connected with a first liquid outlet pipe, and one end, far away from the first water pump, of the first liquid outlet pipe extends into the ultrafiltration tank.
As a further description of the above technical solution:
the upper surface of bottom plate passes through support column fixedly connected with and receives the canister, and receives and strain the left side that the jar is located water pump one, the output fixedly connected with transfer line of water pump one, and the transfer line one end of keeping away from water pump one extends into the inside of receiving the canister, the last fixed surface of bottom plate is connected with water pump two, and the water pump two is located the left side of receiving the canister, the input end fixedly connected with feed liquor pipe two of water pump two.
As a further description of the above technical solution:
one end of the second liquid inlet pipe, far away from the second water pump, extends into the inside of the nanofiltration tank, the output end of the second water pump is fixedly connected with the second liquid outlet pipe, one end of the second liquid outlet pipe, far away from the second water pump, extends into the inside of the heating box, and the side surface of the second liquid outlet pipe is fixedly connected with a control valve.
As a further description of the above technical solution:
the front surface of the nanofiltration tank is fixedly connected with a control box.
The utility model has the following beneficial effects:
1. compared with the prior art, this mineral spring is nanofiltration ultrafiltration liquid concentration and is drawed equipment, pipe and diaphragm through the installation, heat the inside liquid of heating cabinet to the boiling through the electrothermal tube, the steam of production passes through the pipe and meets cold liquefaction to the inside top of handling the case, fall to the inside of drawing the box through the hourglass net and concentrate and draw, the inside of accomplishing the back through the leading-in cooling box of back flow is cooled down, utilize the diaphragm to separate the fender to the liquid of vaporization, it causes the waste to avoid the liquefaction backward flow.
2. Compared with the prior art, this mineral spring is received and is strained concentrated extraction apparatus of ultrafiltration liquid, bull stick and recess through the installation utilize the refrigeration board to carry out the heat transfer to the inside of cooling box, the function drive bull stick through the motor rotates to drive the stirring leaf and rotate, cool down the liquid that the cooling box is inside concentrated and draw, recess through stirring leaf surface makes the stirring leaf increase when the stirring and stirs the degree, improves the concentrated cooling rate who draws good liquid.
3. Compared with the prior art, this mineral spring is received and is strained concentrated extraction equipment of ultrafiltration liquid, through barometer and the discharge valve of installation, utilize the barometer to detect it of jar internal portion, open the discharge valve and reduce pressure when atmospheric pressure exceedes the safety limit of injecing, improve the security of device.
Drawings
FIG. 1 is a schematic diagram of the overall structure of a mineral spring nanofiltration ultrafiltration liquid concentration and extraction device provided by the utility model;
FIG. 2 is a schematic diagram of the front internal structure of the mineral spring nanofiltration ultrafiltration liquid concentration and extraction equipment provided by the utility model;
FIG. 3 is a schematic front view of the mineral spring nanofiltration ultrafiltration liquid concentration and extraction device provided by the utility model;
FIG. 4 is a schematic diagram of the internal structure of the back of the mineral spring nanofiltration ultrafiltration liquid concentration and extraction equipment provided by the utility model;
fig. 5 is a schematic structural diagram of a part A in fig. 2 of the mineral spring nanofiltration ultrafiltration liquid concentration and extraction equipment provided by the utility model.
Illustration of the drawings:
1. a base plate; 2. an ultrafiltration tank; 3. ultrafiltration membranes; 4. an exhaust valve; 5. a liquid inlet pipe I; 6. a booster pump; 7. a first liquid outlet pipe; 8. a first water pump; 9. a transfusion tube; 10. a nanofiltration tank; 11. a barometer; 12. a control box; 13. a liquid inlet pipe II; 14. a second water pump; 15. a second liquid outlet pipe; 16. a control valve; 17. a seat box; 18. a heating box; 19. an electric heating tube; 20. a treatment tank; 21. a conduit; 22. a transverse plate; 23. a leakage net; 24. an extraction box; 25. a return pipe; 26. a cooling box; 27. a motor; 28. a rotating rod; 29. stirring blades; 30. a groove; 31. a drain valve; 32. a temperature sensor; 33. a refrigeration plate.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
In the description of the present invention, it should be noted that the terms "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer", etc., indicate orientations or positional relationships based on the orientations or positional relationships shown in the drawings, and are only for convenience of description and simplicity of description, but do not indicate or imply that the device or element being referred to must have a particular orientation, be constructed and operated in a particular orientation, and thus, should not be construed as limiting the present invention; the terms "first," "second," and "third" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance, and furthermore, unless otherwise explicitly stated or limited, the terms "mounted," "connected," and "connected" are to be construed broadly and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meanings of the above terms in the present invention can be understood in specific cases to those skilled in the art.
Referring to fig. 1-5, the utility model provides a mineral spring nanofiltration ultrafiltration liquid concentration and extraction device: comprises a bottom plate 1, a processing box 20 is fixedly connected with the upper surface of a heating box 18, a guide pipe 21 is arranged in the processing box 20, one end of the guide pipe 21 extends into the heating box 18, a transverse plate 22 is fixedly connected with the side surface of the guide pipe 21, a leakage net 23 is fixedly connected with the side surface of the transverse plate 22, one end of the leakage net 23 far away from the transverse plate 22 is fixedly connected with the inner walls of two sides of the processing box 20, an extraction box 24 is arranged in the processing box 20, the upper surface of the extraction box 24 is fixedly connected with the lower surface of the leakage net 23, a return pipe 25 is fixedly connected with the lower surface of the extraction box 24, a temperature sensor 32 is fixedly connected with the front surface of the processing box 20, an electric heating pipe 19 is arranged in the heating box 18, liquid in the heating box 18 is heated to boiling through the electric heating pipe 19, the generated water vapor is liquefied through the guide pipe 21 and falls into the top of the processing box 20 for concentration and extraction through the leakage net 23, after the liquefaction, the liquid is guided into the cooling box 26 through the return pipe 25 to be cooled, and the vaporized liquid is blocked by the transverse plate 22, so that the waste caused by the liquefaction and the return flow is avoided.
A cooling box 26 is arranged inside the seat box 17, the cooling box 26 is positioned at the left side of the heating box 18, one end of the return pipe 25 far away from the treatment box 20 extends into the cooling box 26, the upper surface of the cooling box 26 is fixedly connected with a motor 27, the output end of the motor 27 is fixedly connected with a rotating rod 28, the rotating rod 28 is positioned in the cooling box 26, the stirring blades 29 are uniformly distributed on the side surface of the rotating rod 28, the front surface of the stirring blades 29 is provided with a groove 30, the rear surface of the cooling box 26 is fixedly connected with a refrigerating plate 33, the refrigerating plate 33 is utilized to transfer heat to the interior of the cooling box 26, the rotation rod 28 is driven to rotate by the operation of the motor 27, thereby driving the stirring blade 29 to rotate, the liquid concentrated and extracted in the cooling box 26 is cooled, and the grooves 30 on the surface of the stirring blades 29 increase the stirring degree of the stirring blades 29 during stirring, so that the cooling speed of the liquid concentrated and extracted is increased.
The inside of ultrafiltration jar 2 is provided with milipore filter 3, the front surface fixedly connected with barometer 11 of ultrafiltration jar 2, the last fixed surface of ultrafiltration jar 2 is connected with discharge valve 4, the last fixed surface of ultrafiltration jar 2 is connected with feed liquor pipe 5, and feed liquor pipe 5 is located discharge valve 4's left side, the side surface fixedly connected with booster pump 6 of feed liquor pipe 5, the stoste passes through the inside of feed liquor pipe 5 input ultrafiltration jar 2, carry out the pressure boost to ultrafiltration jar 2's inside through booster pump 6, make the stoste permeate ultrafiltration membrane 3 fast and fall into jar body bottom, macromolecular impurity that contains in the stoste filters, improve the ultrafiltration efficiency of liquid, utilize barometer 11 to detect jar internal portion's its, open discharge valve 4 when atmospheric pressure exceedes limited safety range and decompress, improve device's security.
Last fixed surface of bottom plate 1 is connected with water pump 8, and water pump 8 is located the left side of ultrafiltration jar 2, input fixedly connected with drain pipe 7 of water pump 8, and drain pipe 7 keeps away from the inside that water pump 8's one end extended into ultrafiltration jar 2, the output fixedly connected with transfer line 9 of water pump 8, and transfer line 9 keeps away from the inside that water pump 8's one end extended into receiving filtration jar 10, flow into drain pipe 7 after the stoste ultrafiltration is accomplished, transfer line 9's inside is put with the stoste pressure that the ultrafiltration is good through water pump 8, send the stoste that the ultrafiltration is good to the inside of nanofiltration jar 10.
The upper surface of the bottom plate 1 is fixedly connected with a nanofiltration tank 10 through a support column, the nanofiltration tank 10 is positioned on the left side of a first water pump 8, the upper surface of the bottom plate 1 is fixedly connected with a second water pump 14, the second water pump 14 is positioned on the left side of the nanofiltration tank 10, the input end of the second water pump 14 is fixedly connected with a second liquid inlet pipe 13, one end, far away from the second water pump 14, of the second liquid inlet pipe 13 extends into the nanofiltration tank 10, the output end of the second water pump 14 is fixedly connected with a second liquid outlet pipe 15, one end, far away from the second water pump 14, of the second liquid outlet pipe 15 extends into a heating box 18, the front surface of the nanofiltration tank 10 is fixedly connected with a control box 12, the stock solution in the nanofiltration tank 10 is subjected to secondary filtration through an adjustment control box 12, small molecular impurities contained in the stock solution are filtered, and the stock solution subjected to nanofiltration in the tank body is pumped into the second liquid inlet pipe 13 through the operation of the second water pump 14 after the filtration is completed, and pressing the solution into a second liquid outlet pipe 15 by using a second water pump 14, so that the stock solution after ultrafiltration and nanofiltration flows into a heating box 18 to be heated and evaporated.
The working principle is as follows: the device comprises a connecting device power supply, stock solution is input into the interior of an ultrafiltration tank 2 through a liquid inlet pipe I5, the interior of the ultrafiltration tank 2 is pressurized through a booster pump 6, the stock solution rapidly penetrates through an ultrafiltration membrane 3 and falls into the bottom of a tank body, macromolecular impurities contained in the stock solution are filtered, the ultrafiltration efficiency of the liquid is improved, the stock solution in the tank body is detected by using a barometer 11, an exhaust valve 4 is opened to reduce pressure when the air pressure exceeds a limited safety range, the safety of the device is improved, the stock solution flows into a liquid outlet pipe I7 after ultrafiltration is completed, the ultrafiltered stock solution is pressed in a liquid conveying pipe 9 through a water pump I8, the ultrafiltered stock solution is conveyed to the interior of a nanofiltration tank 10, the stock solution in the interior of the nanofiltration tank 10 is subjected to secondary filtration through an adjusting control box 12, small molecular impurities contained in the stock solution are filtered, the stock solution after filtration is completed, the stock solution after ultrafiltration is pumped into the interior of the liquid inlet pipe II 13 through the operation of a water pump II 14, the raw liquid after ultrafiltration and nanofiltration is pressed into the liquid outlet pipe II 15 by the water pump II 14, the raw liquid flows into the heating box 18 to be heated and evaporated, the liquid in the heating box 18 is heated to be boiled by the electric heating pipe 19, the generated water vapor is led to the top of the treatment box 20 through the guide pipe 21 to be liquefied, and falls into the extraction box 24 through the leakage net 23 to be concentrated and extracted, and then is led into the cooling box 26 through the return pipe 25 to be cooled, the vaporized liquid is blocked by the transverse plate 22, so that waste caused by liquefied reflux is avoided, the refrigeration plate 33 is used for transferring heat in the cooling box 26, the rotating rod 28 is driven to rotate by the operation of the motor 27, the stirring blades 29 are driven to rotate, the concentrated and extracted liquid in the cooling box 26 is cooled, and the stirring blades 29 are increased in stirring degree by the grooves 30 on the surfaces of the stirring blades 29, the cooling speed of the liquid after concentration and extraction is improved.
Finally, it should be noted that: although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments or portions thereof without departing from the spirit and scope of the utility model.
Claims (8)
1. The mineral spring nanofiltration ultrafiltration liquid concentration and extraction equipment comprises a bottom plate (1), and is characterized in that: a seat box (17) is fixedly connected to the upper surface of the bottom plate (1), a heating box (18) is arranged inside the seat box (17), a treatment box (20) is fixedly connected to the upper surface of the heating box (18), a guide pipe (21) is arranged inside the treatment box (20), and one end of the guide pipe (21) extends into the heating box (18);
the side surface of the guide pipe (21) is fixedly connected with a transverse plate (22), the side surfaces of the transverse plate (22) are fixedly connected with a leakage net (23), and one end of the leakage net (23) far away from the transverse plate (22) is fixedly connected with the inner walls of two sides of the treatment box (20);
an extraction box (24) is arranged in the treatment box (20), the upper surface of the extraction box (24) is fixedly connected with the lower surface of the leakage net (23), and the lower surface of the extraction box (24) is fixedly connected with a return pipe (25);
a cooling box (26) is arranged in the seat box (17), the cooling box (26) is positioned on the left side of the heating box (18), one end, far away from the treatment box (20), of the return pipe (25) extends into the cooling box (26), and the upper surface of the cooling box (26) is fixedly connected with a motor (27);
the output fixedly connected with bull stick (28) of motor (27), and bull stick (28) are located the inside of cooling box (26), the side surface evenly distributed of bull stick (28) has stirring leaf (29), the front surface of stirring leaf (29) is equipped with recess (30).
2. The mineral spring nanofiltration ultrafiltration liquid concentration and extraction equipment according to claim 1, wherein: the back surface of the cooling box (26) is fixedly connected with a refrigeration plate (33), the left side surface of the cooling box (26) is fixedly connected with a liquid discharge valve (31), the front surface of the processing box (20) is fixedly connected with a temperature sensor (32), and an electric heating tube (19) is arranged in the heating box (18).
3. The mineral spring nanofiltration ultrafiltration liquid concentration and extraction equipment according to claim 1, wherein: the upper surface of bottom plate (1) passes through support column fixedly connected with ultrafiltration jar (2), the inside of ultrafiltration jar (2) is provided with milipore filter (3), the front surface fixedly connected with barometer (11) of ultrafiltration jar (2).
4. The mineral spring nanofiltration ultrafiltration liquid concentration and extraction equipment according to claim 3, wherein: the last fixed surface of ultrafiltration jar (2) is connected with discharge valve (4), the last fixed surface of ultrafiltration jar (2) is connected with feed liquor pipe (5), and feed liquor pipe (5) are located the left side of discharge valve (4), the side surface fixedly connected with booster pump (6) of feed liquor pipe (5).
5. The mineral spring nanofiltration ultrafiltration liquid concentration and extraction equipment according to claim 1, wherein: the upper surface fixed connection of bottom plate (1) has water pump (8), and water pump (8) are located the left side of ultrafiltration jar (2), the input end fixedly connected with drain pipe (7) of water pump (8), and the one end that water pump (8) were kept away from in drain pipe (7) extends into the inside of ultrafiltration jar (2).
6. The mineral spring nanofiltration ultrafiltration liquid concentration and extraction equipment according to claim 1, wherein: the upper surface of bottom plate (1) passes through support column fixedly connected with and receives canister (10), and receives canister (10) and be located the left side of water pump (8), output fixedly connected with transfer line (9) of water pump (8), and the one end that water pump (8) were kept away from in transfer line (9) extends into the inside of receiving canister (10), the last fixed surface of bottom plate (1) is connected with two (14) of water pump, and two (14) of water pump are located the left side of receiving canister (10), the input end fixedly connected with feed liquor pipe two (13) of two (14) of water pump.
7. The mineral spring nanofiltration ultrafiltration liquid concentration and extraction equipment according to claim 6, wherein: one end that two (14) of water pump were kept away from in feed liquor pipe two (13) extends into the inside of receiving canister (10), the output end fixedly connected with drain pipe two (15) of two (14) of water pump, and the one end that two (14) of water pump were kept away from in drain pipe two (15) extends into the inside of heating cabinet (18), the side surface fixedly connected with control valve (16) of drain pipe two (15).
8. The mineral spring nanofiltration ultrafiltration liquid concentration and extraction equipment according to claim 6, wherein: the front surface of the nanofiltration tank (10) is fixedly connected with a control box (12).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122093945.0U CN215975380U (en) | 2021-09-01 | 2021-09-01 | Mineral spring nanofiltration ultrafiltration liquid concentration extraction equipment |
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| CN202122093945.0U CN215975380U (en) | 2021-09-01 | 2021-09-01 | Mineral spring nanofiltration ultrafiltration liquid concentration extraction equipment |
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| CN215975380U true CN215975380U (en) | 2022-03-08 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116216997A (en) * | 2023-03-15 | 2023-06-06 | 安徽科博瑞环境科技有限公司 | Iodine contrast agent hydrolysate wastewater concentration and extraction treatment process and system |
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2021
- 2021-09-01 CN CN202122093945.0U patent/CN215975380U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116216997A (en) * | 2023-03-15 | 2023-06-06 | 安徽科博瑞环境科技有限公司 | Iodine contrast agent hydrolysate wastewater concentration and extraction treatment process and system |
| CN116216997B (en) * | 2023-03-15 | 2024-05-28 | 科纳诺流体科技(杭州)有限公司 | Iodine contrast agent hydrolysate wastewater concentration and extraction treatment process and system |
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