CN220034099U - Waste liquid distillation system with jet flow vacuum function - Google Patents
Waste liquid distillation system with jet flow vacuum function Download PDFInfo
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- CN220034099U CN220034099U CN202320914675.1U CN202320914675U CN220034099U CN 220034099 U CN220034099 U CN 220034099U CN 202320914675 U CN202320914675 U CN 202320914675U CN 220034099 U CN220034099 U CN 220034099U
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- fixedly connected
- pipe
- waste liquid
- cold water
- heat exchanger
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- 239000007788 liquid Substances 0.000 title claims abstract description 111
- 239000002699 waste material Substances 0.000 title claims abstract description 60
- 238000004821 distillation Methods 0.000 title claims abstract description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 93
- 238000001704 evaporation Methods 0.000 claims abstract description 29
- 230000008020 evaporation Effects 0.000 claims abstract description 29
- 238000009792 diffusion process Methods 0.000 claims abstract description 16
- 239000010865 sewage Substances 0.000 claims description 15
- 238000007599 discharging Methods 0.000 claims description 9
- 239000008399 tap water Substances 0.000 abstract description 8
- 235000020679 tap water Nutrition 0.000 abstract description 8
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 238000009835 boiling Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000010977 unit operation Methods 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a waste liquid distillation system with a jet flow vacuum function, which comprises a waste liquid evaporation tank and a tap water inlet pipe, wherein one side of the outer surface of the tap water inlet pipe is fixedly connected with a dosing pipe, and one side of the outer surface of the tap water inlet pipe is fixedly connected with a flow guide pipe. This waste liquid distillation system with efflux vacuum function, through the setting of ejector, suction chamber and diffusion room, when specifically using, the cold water pump is collected the water in the cold water tank and is got into in the condenser, carry out the heat exchange through the condenser and become cold water, after carrying out the heat exchange, the exit linkage ejector water inlet of heat exchanger, the ejector spouts the water after with the heat exchange, form the vacuum in the vacuum tube region, thereby will be sucked out by the evacuation medium from the vacuum tube, two-ply medium mixes in the diffusion pipe and energy exchange, make the speed can reduce into pressure energy, with being higher than atmospheric pressure and discharge entering the cold water tank, accomplish the circulation loop of whole pipeline, can produce vacuum again can carry out the heat exchange.
Description
Technical Field
The utility model relates to the technical field of industrial environment-friendly wastewater treatment, in particular to a waste liquid distillation system with a jet flow vacuum function.
Background
Distillation is a thermodynamic separation process, which uses the different boiling points of the components in a mixed liquid or liquid-solid system to evaporate the low boiling components and then condense to separate the whole components, and is a combination of evaporation and condensation unit operations. The existing organic waste liquid is usually recovered and separated from organic matters by distillation. However, the conventional distiller needs stirring to improve heat exchange efficiency during distillation, but the conventional device has a gap between a rotating shaft and a distillation tube, which results in that organic gas is easy to overflow from the gap to corrode a motor and internal current thereof during distillation, resulting in a reduction in the service life of the motor.
Through searching, chinese patent publication (bulletin) No. CN213885029U3 discloses a waste liquid distiller, the patent effectively prevents the corrosion of organic gas to a motor through the arrangement of a closed box body and a rotating shaft, fully utilizes preheating to reduce energy consumption, and also improves the phenomenon that condensation is insufficient due to easy condensation of liquid on the inner wall of a condensing tube, most of waste liquid distilling equipment in the market is high-temperature distillation, but partial vacuum low-temperature distilling equipment is also available, the vacuum low-temperature distilling equipment is widely applied in industry, at present, most of vacuum low-temperature distilling adopts a vacuum pump to perform vacuum work, the vacuum pump is high in price, the use cost of the vacuum pump is high, and a large amount of electric energy is required to be consumed during use, so that the resource consumption is overlarge, and therefore, the design of a waste liquid distilling system with a jet vacuum function is necessary.
Disclosure of Invention
The utility model mainly aims to provide a waste liquid distillation system with a jet flow vacuum function, which can effectively solve the problems in the background technology.
In order to achieve the above purpose, the technical scheme adopted by the utility model is as follows:
the utility model provides a waste liquid distillation system with efflux vacuum function, includes waste liquid evaporation tank and running water inlet tube, surface one side fixedly connected with charge pipe of running water inlet tube, surface one side fixedly connected with honeycomb duct of running water inlet tube, the honeycomb duct is fixedly connected with waste liquid evaporation tank, the one end fixedly connected with cold water tank of honeycomb duct, surface one side fixedly connected with conveyer pipe of cold water tank, surface one side fixedly connected with cold water pump of conveyer pipe, surface one side fixedly connected with water pump pipe of cold water pump, surface one side fixedly connected with condenser of water pump pipe, surface one side fixedly connected with cold water pipe of condenser, surface one side fixedly connected with heat exchanger of cold water pipe; the side fixedly connected with ejector of heat exchanger, heat exchanger is fixed connection with the water inlet of ejector, one side of ejector is provided with first connecting pipe, surface one side fixedly connected with vacuum tube of first connecting pipe, surface one side fixedly connected with diffuser pipe of first connecting pipe, inner wall one side of diffuser pipe is provided with the suction chamber, inner wall one side of diffuser pipe is provided with the diffusion chamber.
In order to enable a water source sprayed by the ejector to enter the cold water tank, the waste liquid distillation system with the jet vacuum function is characterized in that one side of the outer surface of the diffusion pipe is fixedly connected with a second connecting pipe, and the second connecting pipe is fixedly connected with the cold water tank.
In order to perform heat exchange, as the waste liquid distillation system with the jet flow vacuum function, one side of the front surface of the heat exchanger is fixedly connected with a first heat exchange tube, and the first heat exchange tube is fixedly connected with a waste liquid evaporation tank.
In order to enable sewage to be discharged, as the waste liquid distillation system with the jet flow vacuum function, one side of the outer surface of the condenser is fixedly connected with a third connecting pipe, the other end of the third connecting pipe is fixedly connected with a second heat exchanger, one side of the outer surface of the second heat exchanger is fixedly connected with a sewage pipe, one end of the sewage pipe is fixedly connected with a first heat exchanger, and the side surface of the first heat exchanger is fixedly connected with a sewage inlet pipe.
In order to enable the waste liquid distillation system with the jet flow vacuum function to have the condensation function, the other side of the first heat exchanger is fixedly connected with a fourth connecting pipe, and the fourth connecting pipe is fixedly connected with the condenser.
In order to enable the waste liquid to enter the waste liquid evaporation tank, as the waste liquid distillation system with the jet flow vacuum function, one side of the upper surface of the first heat exchanger is fixedly connected with a second heat exchange tube, and the second heat exchange tube is fixedly connected with the waste liquid evaporation tank.
In order to facilitate the discharge of the sewage, as the waste liquid distillation system with the jet flow vacuum function, one side of the outer surface of the waste liquid evaporation tank is fixedly connected with a sewage drain pipe, one side of the outer surface of the sewage drain pipe is provided with a sewage drain valve, one side of the outer surface of the sewage drain pipe is provided with a sewage drain diaphragm pump, and one side of the sewage drain diaphragm pump is fixedly connected with a sewage outlet pipe.
In order to facilitate clear liquid discharge, as the waste liquid distillation system with the jet flow vacuum function, a clear liquid pipe is fixedly connected to one side of the outer surface of the cold water tank, a clear liquid discharge valve is arranged on one side of the outer surface of the clear liquid pipe, a clear liquid discharge pump is arranged on one side of the outer surface of the clear liquid pipe, a liquid outlet pipe is fixedly connected to one side of the back surface of the clear liquid discharge pump, and a flow counter is arranged on one side of the outer surface of the liquid outlet pipe.
Compared with the prior art, the utility model has the following beneficial effects:
in the utility model, through the arrangement of the ejector, the suction chamber and the diffusion chamber, when the device is specifically used, the cold water pump collects water in the cold water tank into the condenser, the condenser is used for heat exchange to be changed into cold water, after the heat exchange is carried out, the outlet of the heat exchanger is connected with the water inlet of the ejector, the ejector ejects the water after the heat exchange, vacuum is formed in the vacuum tube area, thereby sucking the pumped medium out of the vacuum tube, two mediums are mixed and energy exchanged in the diffusion tube, the speed can be reduced into pressure energy, the pressure energy is higher than the atmospheric pressure and the pressure energy is discharged into the cold water tank, and the circulation loop of the whole pipeline is completed, so that vacuum can be generated and the heat exchange can be carried out.
Drawings
FIG. 1 is a schematic elevational view of the present utility model;
FIG. 2 is a schematic view of a part of the structure of the present utility model;
FIG. 3 is a schematic view of a third connecting pipe according to the present utility model;
FIG. 4 is a schematic view of a diffuser pipe according to the present utility model;
FIG. 5 is a second partial schematic view of the present utility model.
In the figure: 1. a waste liquid evaporation tank; 2. a tap water inlet pipe; 3. a dosing tube; 4. a flow guiding pipe; 5. a cold water tank; 6. a delivery tube; 7. a cold water pump; 8. a water pump tube; 9. a condenser; 10. a cold water pipe; 11. a heat exchanger; 12. a jet device; 13. a first connection pipe; 14. a vacuum tube; 15. a diffuser pipe; 16. a suction chamber; 17. a diffusion chamber; 18. a second connection pipe; 19. a first heat exchange tube; 20. a third connection pipe; 21. a second heat exchanger; 22. a dirty liquid pipe; 23. a first heat exchanger; 24. a dirty liquid inlet pipe; 25. a fourth connection pipe; 26. a second heat exchange tube; 27. a blow-down pipe; 28. a sewage discharge diaphragm pump; 29. a sewage outlet pipe; 30. a clear liquid pipe; 31. a clear liquid discharging pump; 32. a liquid outlet pipe; 33. a flow rate counter.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
As shown in fig. 1-5, a waste liquid distillation system with jet vacuum function comprises a waste liquid evaporation tank 1 and a tap water inlet pipe 2, wherein a dosing pipe 3 is fixedly connected to one side of the outer surface of the tap water inlet pipe 2, a flow guide pipe 4 is fixedly connected to one side of the outer surface of the tap water inlet pipe 2, the flow guide pipe 4 is fixedly connected with the waste liquid evaporation tank 1, one end of the flow guide pipe 4 is fixedly connected with a cold water tank 5, a conveying pipe 6 is fixedly connected to one side of the outer surface of the cold water tank 5, a cold water pump 7 is fixedly connected to one side of the outer surface of the conveying pipe 6, a water pump pipe 8 is fixedly connected to one side of the upper surface of the cold water pump 7, a condenser 9 is fixedly connected to one side of the outer surface of the water pump pipe 8, a cold water pipe 10 is fixedly connected to one side of the outer surface of the cold water pipe 10, and a heat exchanger 11 is fixedly connected to one side of the outer surface of the cold water pipe 10;
in this embodiment, the side of the heat exchanger 11 is fixedly connected with the ejector 12, the heat exchanger 11 is fixedly connected with the water inlet of the ejector 12, one side of the ejector 12 is provided with the first connecting pipe 13, one side of the outer surface of the first connecting pipe 13 is fixedly connected with the vacuum pipe 14, one side of the outer surface of the first connecting pipe 13 is fixedly connected with the diffuser pipe 15, one side of the inner wall of the diffuser pipe 15 is provided with the suction chamber 16, and one side of the inner wall of the diffuser pipe 15 is provided with the diffuser chamber 17.
When the condenser is specifically used, after cold water entering the heat exchanger 11 from the condenser 9 is subjected to heat exchange in the heat exchanger 11, the outlet of the heat exchanger 11 is connected with the water inlet of the ejector 12, the ejector 12 ejects the water subjected to heat exchange, vacuum is formed in the outlet area of the nozzle, so that pumped media are sucked out of the vacuum tube 14, two media are mixed and subjected to energy exchange in the diffuser pipe 15, the speed energy is reduced to pressure energy, and finally the pressure energy is discharged into the cold water tank 5 under the pressure higher than the atmospheric pressure, and the circulation loop of the whole pipeline is completed.
In this embodiment, a second connection pipe 18 is fixedly connected to one side of the outer surface of the diffuser pipe 15, and the second connection pipe 18 is fixedly connected to the cold water tank 5.
In specific use, the ejector 12 ejects the water after heat exchange, and vacuum is formed in the outlet area of the nozzle, so that the pumped medium is sucked out from the vacuum tube 14, the two mediums are mixed and energy exchanged in the diffuser 15, and finally discharged into the second connecting tube 18 at high and atmospheric pressure, and then enter the cold water tank 5.
In this embodiment, a first heat exchange tube 19 is fixedly connected to one side of the front surface of the heat exchanger 11, and the first heat exchange tube 19 is fixedly connected to the waste liquid evaporation tank 1.
In specific use, the water vapor after evaporation in the waste liquid evaporation tank 1 enters the heat exchanger 11 through the first heat exchange tube 19, and enters the ejector 12 for medium mixing and energy conversion after heat exchange.
In this embodiment, a third connecting pipe 20 is fixedly connected to one side of the outer surface of the condenser 9, a second heat exchanger 21 is fixedly connected to the other end of the third connecting pipe 20, a dirty liquid pipe 22 is fixedly connected to one side of the outer surface of the second heat exchanger 21, a first heat exchanger 23 is fixedly connected to one end of the dirty liquid pipe 22, and a dirty liquid inlet pipe 24 is fixedly connected to the side surface of the first heat exchanger 23.
When the device is specifically used, the dirty liquid is conveyed to the dirty liquid pipe 22 through the dirty liquid water inlet pipe 24 and flows into the first heat exchanger 23, the dirty liquid is discharged into the condenser 9 after heat exchange in the first heat exchanger 23, and the dirty liquid after heat exchange enters into the second heat exchanger 21 through the dirty liquid pipe 22.
In this embodiment, a fourth connecting pipe 25 is fixedly connected to the other side of the first heat exchanger 23, and the fourth connecting pipe 25 is fixedly connected to the condenser 9.
In a specific use, the contaminated liquid enters the condenser 9 through the fourth connection pipe 25 after heat exchange in the first heat exchanger 23.
In this embodiment, a second heat exchange tube 26 is fixedly connected to one side of the upper surface of the first heat exchanger 23, and the second heat exchange tube 26 is fixedly connected to the waste liquid evaporation tank 1.
In specific use, the second heat exchange tube 26 is fixedly connected with the waste liquid evaporation tank 1, and water in the second heat exchange tube 26 can be discharged into the waste liquid evaporation tank 1.
In this embodiment, a drain pipe 27 is fixedly connected to one side of the outer surface of the waste liquid evaporation tank 1, a drain valve is arranged on one side of the outer surface of the drain pipe 27, a drain diaphragm pump 28 is mounted on one side of the outer surface of the drain pipe 27, and a drain pipe 29 is fixedly connected to one side of the drain diaphragm pump 28.
When the waste liquid evaporator is particularly used, after the drain valve is opened, the drain diaphragm pump 28 is started, and the drain pipe 27 can drain the waste liquid in the waste liquid evaporator 1 out of the waste liquid evaporator 1 through the drain diaphragm pump 28.
In this embodiment, a clear liquid pipe 30 is fixedly connected to one side of the outer surface of the cold water tank 5, a clear liquid discharging valve is arranged on one side of the outer surface of the clear liquid pipe 30, a clear liquid discharging pump 31 is installed on one side of the outer surface of the clear liquid pipe 30, a liquid outlet pipe 32 is fixedly connected to one side of the back surface of the clear liquid discharging pump 31, and a flow rate statistics device 33 is installed on one side of the outer surface of the liquid outlet pipe 32.
When the device is specifically used, after the clear liquid discharging valve is opened, the clear liquid in the cold water tank 5 is pumped by the clear liquid discharging pump 31 and discharged through the liquid outlet pipe 32, and the flow rate statistics device 33 can count the water amount discharged by the clear liquid.
Working principle: in use, water is discharged to the waste liquid evaporation tank 1 through the tap water inlet pipe 2, the waste liquid evaporation tank 1 is connected with the cold water tank 5 through the guide pipe 4, the water in the cold water tank 5 is from steam condensate generated by the waste liquid evaporation tank 1, the cold water tank 5 is connected with the cold water pump 7 through the conveying pipe 6, the cold water pump 7 is connected with the condenser 9 through the water pump pipe 8, and the condenser 9 mainly reduces the water temperature of the cold water tank 5 so as to exchange heat with steam, so that distilled water is obtained. The condenser 9 is connected with the heat exchanger 11 through the cold water pipe 10, the heat exchanger 11 is connected with the water inlet of the ejector 12, after the ejector 12 ejects water source, working fluid with certain pressure is ejected at high speed through the water outlet of the ejector 12, pumped media in the waste liquid evaporation tank 1 are sucked out through the vacuum pipe 14 when passing through the first connecting pipe 13, the waste liquid evaporation tank enters the diffusion pipe 15 through the first connecting pipe 13, the waste liquid evaporation tank enters the diffusion chamber 17 through the suction chamber 16, two media are mixed and energy-converted in the diffusion pipe 15, the speed can be reduced into pressure energy, and finally the pressure energy is discharged by being higher than the atmospheric pressure, the second connecting pipe 18 is connected with the diffusion pipe 15 and the cold water tank 5, so that the water source ejected by the ejector 12 enters the cold water tank 5 to complete a loop.
The foregoing has shown and described the basic principles and main features of the present utility model and the advantages of the present utility model. It will be understood by those skilled in the art that the present utility model is not limited to the embodiments described above, and that the above embodiments and descriptions are merely illustrative of the principles of the present utility model, and various changes and modifications may be made without departing from the spirit and scope of the utility model, which is defined in the appended claims. The scope of the utility model is defined by the appended claims and equivalents thereof.
Claims (8)
1. The utility model provides a waste liquid distillation system with efflux vacuum function, includes waste liquid evaporation tank (1) and running water inlet tube (2), its characterized in that: the utility model discloses a cold water treatment device, including running water inlet tube (2), cold water inlet tube (5), cold water pump (7), condenser (9), cold water pipe (10) and heat exchanger (11) respectively, outer surface side fixedly connected with of cold water pipe (5) and delivery pipe (6), outer surface side fixedly connected with dosing tube (3) of running water inlet tube (2), outer surface side fixedly connected with honeycomb duct (4) of running water inlet tube (2), honeycomb duct (4) are fixedly connected with waste liquid evaporation jar (1), one end fixedly connected with cold water tank (5) of honeycomb duct (4), outer surface side fixedly connected with conveyer pipe (6) of cold water tank (5), upper surface side fixedly connected with water pump (8) of cold water pump (7), outer surface side fixedly connected with condenser (9) of water pump (8), outer surface side fixedly connected with cold water pipe (10) of condenser (11);
the side fixedly connected with ejector (12) of heat exchanger (11), heat exchanger (11) are fixed connection with the water inlet of ejector (12), one side of ejector (12) is provided with first connecting pipe (13), surface one side fixedly connected with vacuum tube (14) of first connecting pipe (13), surface one side fixedly connected with diffusion pipe (15) of first connecting pipe (13), the inner wall one side of diffusion pipe (15) is provided with suction chamber (16), the inner wall one side of diffusion pipe (15) is provided with diffusion chamber (17).
2. A waste liquid distillation system having a jet vacuum function according to claim 1, wherein: a second connecting pipe (18) is fixedly connected to one side of the outer surface of the diffusion pipe (15), and the second connecting pipe (18) is fixedly connected with the cold water tank (5).
3. A waste liquid distillation system having a jet vacuum function according to claim 1, wherein: the waste liquid evaporator is characterized in that a first heat exchange tube (19) is fixedly connected to one side of the front face of the heat exchanger (11), and the first heat exchange tube (19) is fixedly connected with the waste liquid evaporator (1).
4. A waste liquid distillation system having a jet vacuum function according to claim 1, wherein: the condenser is characterized in that a third connecting pipe (20) is fixedly connected to one side of the outer surface of the condenser (9), a second heat exchanger (21) is fixedly connected to the other end of the third connecting pipe (20), a dirty liquid pipe (22) is fixedly connected to one side of the outer surface of the second heat exchanger (21), a first heat exchanger (23) is fixedly connected to one end of the dirty liquid pipe (22), and a dirty liquid inlet pipe (24) is fixedly connected to the side face of the first heat exchanger (23).
5. The waste liquid distillation system with jet vacuum function according to claim 4, wherein: the other side of the first heat exchanger (23) is fixedly connected with a fourth connecting pipe (25), and the fourth connecting pipe (25) is fixedly connected with the condenser (9).
6. The waste liquid distillation system with jet vacuum function according to claim 4, wherein: a second heat exchange tube (26) is fixedly connected to one side of the upper surface of the first heat exchanger (23), and the second heat exchange tube (26) is fixedly connected with the waste liquid evaporation tank (1).
7. A waste liquid distillation system having a jet vacuum function according to claim 1, wherein: the waste liquid evaporation tank is characterized in that a drain pipe (27) is fixedly connected to one side of the outer surface of the waste liquid evaporation tank (1), a drain valve is arranged on one side of the outer surface of the drain pipe (27), a drain diaphragm pump (28) is arranged on one side of the outer surface of the drain pipe (27), and a sewage outlet pipe (29) is fixedly connected to one side of the drain diaphragm pump (28).
8. A waste liquid distillation system having a jet vacuum function according to claim 1, wherein: the device is characterized in that a clear liquid pipe (30) is fixedly connected to one side of the outer surface of the cold water tank (5), a clear liquid discharging valve is arranged on one side of the outer surface of the clear liquid pipe (30), a clear liquid discharging pump (31) is arranged on one side of the outer surface of the clear liquid pipe (30), a liquid outlet pipe (32) is fixedly connected to one side of the back of the clear liquid discharging pump (31), and a flow counter (33) is arranged on one side of the outer surface of the liquid outlet pipe (32).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320914675.1U CN220034099U (en) | 2023-04-21 | 2023-04-21 | Waste liquid distillation system with jet flow vacuum function |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320914675.1U CN220034099U (en) | 2023-04-21 | 2023-04-21 | Waste liquid distillation system with jet flow vacuum function |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220034099U true CN220034099U (en) | 2023-11-17 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202320914675.1U Active CN220034099U (en) | 2023-04-21 | 2023-04-21 | Waste liquid distillation system with jet flow vacuum function |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220034099U (en) |
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2023
- 2023-04-21 CN CN202320914675.1U patent/CN220034099U/en active Active
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