CN210751677U - High-efficient waste liquid enrichment facility - Google Patents
High-efficient waste liquid enrichment facility Download PDFInfo
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- CN210751677U CN210751677U CN201921162550.8U CN201921162550U CN210751677U CN 210751677 U CN210751677 U CN 210751677U CN 201921162550 U CN201921162550 U CN 201921162550U CN 210751677 U CN210751677 U CN 210751677U
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Abstract
The utility model discloses a high-efficient waste liquid enrichment facility, disconnect-type dust removal deoiling fog whirl board tower main part, condenser, heat exchanger, high-efficient exhaust fan, compressor, condenser and high-efficient exhaust fan all are located disconnect-type dust removal deoiling fog whirl board tower main part one side. When waste gas will enter into the condenser through an exhaust pipe after the separation type dust removal oil mist removal rotating plate tower main part purifies filtration layer by layer, steam to in the waste gas advances the condensation operation, and condensate accessible comdenstion water discharge port after the condensation outwards discharges, waste gas after the condensation will be taken out to No. three exhaust pipes by its high-efficient exhaust fan through No. two exhaust pipes, enter into the heat exchanger at last, thereby heat exchanger heats its waste gas again, produce steam, and enter into separation type dust removal oil mist removal rotating plate tower main part again through waste gas entry and carry out the recirculation, thereby can play high-efficient concentration effect.
Description
Technical Field
The utility model relates to a enrichment facility specifically is a high-efficient waste liquid enrichment facility.
Background
At present, environmental protection in environmental protection methods has been established as a basic national policy in China. As wastewater treatment in environmental protection, the discharge standard of industrial wastewater treatment is becoming more and more strict, the existing industrial wastewater treatment technology faces huge challenges, in the original technology, high hazardous waste disposal cost brings great economic pressure to enterprises, and as a key technology in waste liquid treatment, waste liquid reduction treatment becomes a key point of current attention.
However, the conventional waste liquid concentrating apparatus has low concentration efficiency and cannot perform reciprocating reflux concentration. Accordingly, those skilled in the art have provided an efficient waste liquid concentrating apparatus to solve the above-mentioned problems of the background art.
Disclosure of Invention
An object of the utility model is to provide a high-efficient waste liquid enrichment facility to solve the problem that proposes in the above-mentioned background art.
In order to achieve the above object, the utility model provides a following technical scheme:
the utility model provides a high-efficient waste liquid enrichment facility, disconnect-type dust removal deoiling fog whirl board tower main part, condenser, heat exchanger, high-efficient exhaust fan, compressor, condenser and high-efficient exhaust fan all are located disconnect-type dust removal deoiling fog whirl board tower main part one side, heat exchanger and compressor all are located department between disconnect-type dust removal deoiling fog whirl board tower main part and condenser and the high-efficient exhaust fan, are connected with the exhaust pipe No. one between disconnect-type dust removal deoiling fog whirl board tower main part and the condenser, are connected with the exhaust pipe No. two between condenser and the high-efficient exhaust fan, are connected with the exhaust pipe No. three between heat exchanger and the high-efficient exhaust fan, are connected with the exhaust pipe No. four between heat exchanger and the disconnect-type dust removal deoiling fog whirl board tower main part, the compressor respectively with the condenser, all through copper pipe.
When waste gas will enter into the condenser through an exhaust pipe after the separation type dust removal oil mist removal rotating plate tower main part purifies filtration layer by layer, steam to in the waste gas advances the condensation operation, and condensate accessible comdenstion water discharge port after the condensation outwards discharges, waste gas after the condensation will be taken out to No. three exhaust pipes by its high-efficient exhaust fan through No. two exhaust pipes, enter into the heat exchanger at last, thereby heat exchanger heats its waste gas again, produce steam, and enter into separation type dust removal oil mist removal rotating plate tower main part again through waste gas entry and carry out the recirculation, thereby can play high-efficient concentration effect.
As a further aspect of the present invention: the upper end of the separated dust and oil removing mist rotating plate tower body is provided with a waste gas outlet, and one side of the separated dust and oil removing mist rotating plate tower body is provided with a waste gas inlet.
As a further aspect of the present invention: the heat exchanger and the compressor are vertically symmetrical, and the condenser and the high-efficiency exhaust fan are vertically symmetrical.
As a further aspect of the present invention: the lower end of the condenser is provided with a condensed water discharge port, and the lower end of the heat exchanger is provided with a water discharge port.
As a further aspect of the present invention: a fresh air supplementing opening is inserted into one side of the second exhaust pipe in a penetrating mode, and a fresh air supplementing adjusting valve is arranged on the fresh air supplementing opening.
As a further aspect of the present invention: the separating type dust and oil removing mist rotating plate tower body is fixedly connected with a first exhaust pipe through a waste gas outlet, and the separating type dust and oil removing mist rotating plate tower body is fixedly connected with a fourth exhaust pipe through a waste gas inlet.
Compared with the prior art, the beneficial effects of the utility model are that:
when waste gas will enter into the condenser through an exhaust pipe after the separation type dust removal oil mist removal rotating plate tower main part purifies filtration layer by layer, steam to in the waste gas advances the condensation operation, and condensate accessible comdenstion water discharge port after the condensation outwards discharges, waste gas after the condensation will be taken out to No. three exhaust pipes by its high-efficient exhaust fan through No. two exhaust pipes, enter into the heat exchanger at last, thereby heat exchanger heats its waste gas again, produce steam, and enter into separation type dust removal oil mist removal rotating plate tower main part again through waste gas entry and carry out the recirculation, thereby can play high-efficient concentration effect.
Drawings
Fig. 1 is a schematic structural diagram of a high-efficiency waste liquid concentrating device.
In the figure: 1. a separated dust and oil mist removing rotating plate tower main body; 2. an exhaust gas outlet; 3. an exhaust gas inlet; 4. a condenser; 5. a heat exchanger; 6. a condensed water discharge port; 7. a water outlet; 8. a fresh air supplementing opening; 9. fresh air supplementing regulating valves; 10. a first exhaust duct; 11. a high-efficiency exhaust fan; 12. a compressor; 13. a second exhaust pipe; 14. a third exhaust pipe; 15. and a fourth exhaust pipe.
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. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1, in an embodiment of the present invention, a high-efficiency waste liquid concentrating device includes a separating type dust and oil removing cyclone plate tower main body 1, a condenser 4, a heat exchanger 5, a high-efficiency exhaust fan 11, and a compressor 12, wherein the condenser 4 and the high-efficiency exhaust fan 11 are both located at one side of the separating type dust and oil removing cyclone plate tower main body 1, the heat exchanger 5 and the compressor 12 are both located between the separating type dust and oil removing cyclone plate tower main body 1 and the condenser 4 and the high-efficiency exhaust fan 11, a first exhaust pipe 10 is connected between the separating type dust and oil removing cyclone plate tower main body 1 and the condenser 4, a second exhaust pipe 13 is connected between the condenser 4 and the high-efficiency exhaust fan 11, a third exhaust pipe 14 is connected between the heat exchanger 5 and the separating type dust and oil removing cyclone plate tower main body 11, a fourth exhaust pipe 15 is connected between the heat exchanger 5 and the separating type dust and oil removing cyclone plate tower main body 1, the heat exchangers 5 are fixedly connected through copper pipes.
When waste gas will enter into condenser 4 through exhaust pipe 10 after 1 layer of purification filtration of disconnect-type dust removal deoiling fog whirl board tower main part, the steam to in the waste gas advances the condensation operation, and condensate accessible comdenstion water discharge port 6 after the condensation is outwards discharged, waste gas after the condensation will be taken out to No. three exhaust pipes 14 by its high-efficient exhaust fan 11 through No. two exhaust pipes 13, enter into heat exchanger 5 at last, thereby heat exchanger 5 heats its waste gas again, produce steam, and enter into disconnect-type dust removal deoiling fog whirl board tower main part 1 again through waste gas entry 3 and carry out the recirculation, thereby can play high-efficient concentration effect.
The upper end of the separated dust and oil removing mist rotating plate tower body 1 is provided with a waste gas outlet 2, and one side of the separated dust and oil removing mist rotating plate tower body 1 is provided with a waste gas inlet 3.
The heat exchanger 5 and the compressor 12 are vertically symmetrical, and the condenser 4 and the high-efficiency exhaust fan 11 are vertically symmetrical.
The lower end of the condenser 4 is provided with a condensed water discharge port 6, and the lower end of the heat exchanger 5 is provided with a water discharge port 7.
A fresh air supplementing opening 8 is inserted into one side of the second exhaust pipe 13 in a penetrating mode, and a fresh air supplementing adjusting valve 9 is arranged on the fresh air supplementing opening 8.
Disconnect-type dust removal deoiling fog whirl board tower main part 1 passes through exhaust outlet 2 and exhaust pipe 10 fixed connection No. one, and disconnect-type dust removal deoiling fog whirl board tower main part 1 passes through waste gas entry 3 and 15 fixed connection of No. four exhaust pipes.
The utility model discloses a theory of operation is:
when waste gas will enter into condenser 4 through exhaust pipe 10 after 1 layer of purification filtration of disconnect-type dust removal deoiling fog whirl board tower main part, the steam to in the waste gas advances the condensation operation, and condensate accessible comdenstion water discharge port 6 after the condensation is outwards discharged, waste gas after the condensation will be taken out to No. three exhaust pipes 14 by its high-efficient exhaust fan 11 through No. two exhaust pipes 13, enter into heat exchanger 5 at last, thereby heat exchanger 5 heats its waste gas again, produce steam, and enter into disconnect-type dust removal deoiling fog whirl board tower main part 1 again through waste gas entry 3 and carry out the recirculation, thereby can play high-efficient concentration effect.
The above, only be the concrete implementation of the preferred embodiment of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art is in the technical scope of the present invention, according to the technical solution of the present invention and the utility model, the concept of which is equivalent to replace or change, should be covered within the protection scope of the present invention.
Claims (6)
1. The utility model provides a high-efficient waste liquid enrichment facility, its characterized in that, disconnect-type dust removal deoiling fog whirl board tower main part (1), condenser (4), heat exchanger (5), high-efficient exhaust fan (11), compressor (12), condenser (4) and high-efficient exhaust fan (11) all are located disconnect-type dust removal deoiling fog whirl board tower main part (1) one side, and heat exchanger (5) and compressor (12) all are located the disconnect-type dust removal deoiling fog whirl board tower main part (1) and locate between condenser (4) and high-efficient exhaust fan (11), are connected with No. one exhaust pipe (10) between disconnect-type dust removal deoiling fog whirl board tower main part (1) and condenser (4), are connected with No. two exhaust pipe (13) between condenser (4) and high-efficient exhaust fan (11), are connected with No. three exhaust pipe (14) between heat exchanger (5) and high-efficient exhaust fan (11), are connected with No. four exhaust pipe (5) between disconnect-type dust removal deoiling fog whirl board tower main part (1) and the heat exchanger (5 (15) The compressor (12) is fixedly connected with the condenser (4) and the heat exchanger (5) through copper pipes.
2. The high-efficiency waste liquid concentrating device according to claim 1, wherein the upper end of the separated dust and oil removing mist rotating plate tower body (1) is provided with a waste gas outlet (2), and one side of the separated dust and oil removing mist rotating plate tower body (1) is provided with a waste gas inlet (3).
3. The apparatus for concentrating high efficiency waste liquid according to claim 1, wherein the heat exchanger (5) and the compressor (12) are vertically symmetrical, and the condenser (4) and the high efficiency exhaust fan (11) are vertically symmetrical.
4. A high efficiency waste liquid concentrator as claimed in claim 1, wherein the condenser (4) is provided with a condensed water discharge port (6) at the lower end thereof, and the heat exchanger (5) is provided with a water discharge port (7) at the lower end thereof.
5. The high-efficiency waste liquid concentrating device according to claim 1, wherein a fresh air supply port (8) is inserted into one side of the second exhaust pipe (13), and a fresh air supply regulating valve (9) is arranged on the fresh air supply port (8).
6. The high-efficiency waste liquid concentrating device according to claim 1, wherein the separated dust and oil mist removing rotating plate tower body (1) is fixedly connected with the first exhaust pipe (10) through the waste gas outlet (2), and the separated dust and oil mist removing rotating plate tower body (1) is fixedly connected with the fourth exhaust pipe (15) through the waste gas inlet (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921162550.8U CN210751677U (en) | 2019-07-23 | 2019-07-23 | High-efficient waste liquid enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921162550.8U CN210751677U (en) | 2019-07-23 | 2019-07-23 | High-efficient waste liquid enrichment facility |
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| Publication Number | Publication Date |
|---|---|
| CN210751677U true CN210751677U (en) | 2020-06-16 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201921162550.8U Active CN210751677U (en) | 2019-07-23 | 2019-07-23 | High-efficient waste liquid enrichment facility |
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| CN (1) | CN210751677U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110433573A (en) * | 2019-07-23 | 2019-11-12 | 昆山钛锟环保节能科技有限公司 | Efficient waste liquid enrichment facility |
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2019
- 2019-07-23 CN CN201921162550.8U patent/CN210751677U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110433573A (en) * | 2019-07-23 | 2019-11-12 | 昆山钛锟环保节能科技有限公司 | Efficient waste liquid enrichment facility |
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Address after: 215000 No.2 factory building, 285 Chengxiang Road, Bacheng Town, Kunshan City, Suzhou City, Jiangsu Province Patentee after: Suzhou tikun environmental protection and energy saving Technology Co.,Ltd. Address before: 215000 room 4, No.5 Huasheng East Road, Zhoushi Town, Kunshan City, Suzhou City, Jiangsu Province Patentee before: KUNSHAN TAI KUN ENVIRONMENTAL PROTECTION ENERGY SAVING TECHNOLOGY Co.,Ltd. |