CN109734147A - A kind of water process evaporation reclamation set - Google Patents
A kind of water process evaporation reclamation set Download PDFInfo
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- CN109734147A CN109734147A CN201910161060.4A CN201910161060A CN109734147A CN 109734147 A CN109734147 A CN 109734147A CN 201910161060 A CN201910161060 A CN 201910161060A CN 109734147 A CN109734147 A CN 109734147A
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Abstract
The invention discloses a kind of water process to evaporate reclamation set, including cabinet, the gas-liquid process chamber of one S-shaped closed loop is installed in cabinet, gas-liquid process chamber is provided with the spray chamber that head and the tail are sequentially communicated, waste liquid separation chamber, gas converting heat room and water purification recovery room, the filter residue detached job of waste liquid separation chamber progress waste liquid, gas converting heat room and water purification recovery room are then used to recycle the water purification for having filtered waste residue, it is directly to utilize field of air conditioning Refrigeration Technique principle, heating heating is carried out to waste liquid using its heat generated, cold air obtained carries out condensing recovery to vapor, it not only heats but also freezes under unit quantity of electricity, make full use of electric energy, energy consumption is than high；In addition the gas-liquid of closed loop handles circulating internal air to handle the waste water after atomization; by in the waste water after atomization waste residue and water purification separate; utilization is separately recovered in water purification and waste residue; entire waste water atomization process, the process of separation take full advantage of electric energy; energy-saving effect is good; exhaust gas will not leak in treatment process, protect environment.
Description
Technical field
The present invention relates to water-treatment technology field, in particular to a kind of water process evaporates reclamation set.
Background technique
Plating is exactly to plate the process of the other metal or alloy of a thin layer on certain metal surfaces using electrolysis principle, is
The technique of the surface of metal or other materials product attachment layer of metal film is set to prevent metal oxygen to play using electrolysis
The effects of changing (as corroded), improving wearability, electric conductivity, reflective, corrosion resistance (copper sulphate etc.) and having improved aesthetic appearance, extensively
Applied to it is various life or industrial goods on, be very important a kind of technique in modern crafts, but be electroplated generate sewage (such as
Lose the electrolyte of effectiveness) be water pollution important sources, existing some electroplating sewerage processing equipments are mostly using evaporating back
The method of receipts, this method be electroplating wastewater is electrically heated or burner heating method evaporation, keep heavy metal wastewater thereby dense
Contracting, and a kind of processing method recycled, the plating for applying in general to handle containing chromium, copper, silver, nickel etc. containing heavy metal are useless
Water, it has the shortcomings that, and energy consumption is high, it is at high cost, take up a large area, running expense it is high, and the condensing recovery water that evaporates of waste.
Summary of the invention
For overcome the deficiencies in the prior art, the present invention provides a kind of of simple structure and low cost, less energy consumption water process
Evaporate reclamation set.
The technical solution adopted by the present invention to solve the technical problems is:
A kind of water process evaporates reclamation set, including cabinet, and the gas-liquid process chamber of a S-shaped closed loop is equipped in the cabinet,
The gas-liquid process chamber is provided with spray chamber, waste liquid separation chamber, gas converting heat room and the water purification recovery room that head and the tail are sequentially communicated, institute
The upper end for stating waste liquid separation chamber and water purification recovery room is additionally provided with circulating cold air room, and the upper end of the spray chamber is equipped with axis stream wind
Machine and Waste liquid atomization entrance, the Waste liquid atomization entrance are arranged at the air outlet of the axial flow blower, the waste liquid separation chamber
Middle part the first solid-liquid separator is installed, the gas converting heat indoor location has a gas heat exchanger, the gas heat exchanger
It is provided with intersection and mutually the hot gas runner and cold air runner of connection, the hot gas runner is not connected to the gas converting heat room, institute
It states cold air runner to be connected to the circulating cold air room, the outlet of the circulating cold air room connects with the air inlet of the axial flow blower
Logical, the bottom of the water purification recovery room is provided with water purification water outlet, and condenser and second is equipped in the water purification recovery room and is consolidated
Liquid/gas separator, the condenser are provided with several condensate liquid runners for being alternatively arranged and interconnecting, also pacify on the cabinet
Intersect pipe heat exchanger, the second intersection pipe heat exchanger, compressor, refrigerant circulation pump and condensed water equipped with condensation water tank, first
Circulating pump, the first intersection pipe heat exchanger, which is provided with, not to be connected to but adjacent the first refrigerant channel and waste liquid runner mutually, institute
It states the second intersection pipe heat exchanger and is provided with and be not connected to but adjacent the second refrigerant channel and condensed water runner mutually, described first is cold
Matchmaker's runner, compressor, refrigerant circulation pump, the second refrigerant channel head and the tail are sequentially communicated and internal filling flowing has refrigerant, described cold
Condensation tank, condensate water circulatory pump, condensed water runner and condensate liquid runner head and the tail are sequentially communicated and internal filling flowing has condensed water,
The outlet of the waste liquid runner is connected to the Waste liquid atomization entrance, and the entrance of the waste liquid runner is in communication with the outside.
The water purification recovery room is provided with end to end two, and two water purification recovery rooms are arranged side by side setting, and two
The lower end of a water purification recovery room is provided with water purification collecting chamber, is provided between two water purification recovery rooms to the water purification
The partition that collecting chamber extends, the bottom of the partition and the water purification collecting chamber are tightly connected, the side of the partition with it is described
Airflow-reversing mouth is provided between water purification collecting chamber.
First solid-liquid separator and the second solid-liquid separator are several wave-shape boards arranged in parallel, the wave
Plate is provided with the solid recoverer of protrusion.
A liquid separatnig plate is also equipped between the spray chamber, waste liquid separation chamber.
The exhausted bath box being connected to the entrance of the waste liquid runner, the waste liquid separation chamber setting are also equipped on the cabinet
There is the devil liquor recovery pipe being connected to the exhausted bath box, water pump is installed in the exhausted bath box.
The beneficial effects of the present invention are: water process of the invention evaporates reclamation set, including cabinet, one is equipped in cabinet
The gas-liquid process chamber of S-shaped closed loop, gas-liquid process chamber are provided with spray chamber, waste liquid separation chamber, the gas that head and the tail are sequentially communicated and change
The upper end of hot cell and water purification recovery room, waste liquid separation chamber and water purification recovery room is additionally provided with circulating cold air room, the upper end of spray chamber
Axial flow blower and Waste liquid atomization entrance be installed, waste liquid separation chamber carries out the filter residue detached job of waste liquid, gas converting heat room and net
Water recovery room is then used to recycle the water purification for having filtered waste residue, is directly using field of air conditioning Refrigeration Technique principle, using generation
Heat carries out heating heating to waste liquid, and cold air obtained carries out condensing recovery to vapor, not only heated but also freezed under unit quantity of electricity,
Electric energy is made full use of, energy consumption is than high；In addition the gas-liquid of closed loop handles circulating internal air to handle the waste water after atomization, incites somebody to action
Waste residue in waste water and water purification after atomization separate, and utilization, entire waste water atomization process, separation is separately recovered in water purification and waste residue
Process take full advantage of the electric energy of compressor refrigeration, energy-saving effect is good, and since gas-liquid process chamber is enclosed environment,
Gas caused by waste liquid hardly leaks, and will not pollute air, environmental-friendly, and wastewater treatment process is simple, direct, energy consumption
It is few.
Detailed description of the invention
Present invention will be further explained below with reference to the attached drawings and examples.
Fig. 1 is structural schematic diagram of the invention；
Fig. 2 is structure sectional view of the invention；
Fig. 3 is the structural schematic diagram of the first solid-liquid separator and the second solid-liquid separator.
Specific embodiment
Referring to figs. 1 to Fig. 3, a kind of water process evaporates reclamation set, including cabinet 1, and one is equipped in the cabinet 1 in S
The gas-liquid process chamber of shape closed loop, the gas-liquid process chamber are provided with spray chamber 2, the waste liquid separation chamber 3, gas that head and the tail are sequentially communicated
The upper end of Heat Room 5 and water purification recovery room 4, the waste liquid separation chamber 3 and water purification recovery room 4 is additionally provided with circulating cold air room 6, institute
The upper end for stating spray chamber 2 is equipped with axial flow blower 7 and Waste liquid atomization entrance 8, and the Waste liquid atomization entrance 8 is arranged in the axis stream
At the air outlet of blower 7, the middle part of the waste liquid separation chamber 3 is equipped with the first solid-liquid separator 9, in the gas converting heat room 5
One gas heat exchanger 10 is installed, the gas heat exchanger 10 is provided with the hot gas runner and cold air runner of intersection and mutual not connection
11, the hot gas runner is connected to the gas converting heat room 5, and the cold air runner is connected to the circulating cold air room 6, described cold
The outlet of gas circular chamber 6 is connected to the air inlet of the axial flow blower 7, and the bottom of the water purification recovery room 4 is provided with water purification
Water outlet 12 is equipped with condenser 13 and the second solid-liquid separator 14 in the water purification recovery room 4, and the condenser 13 is provided with
Several condensate liquid runners 15 for being alternatively arranged and interconnecting are also equipped with the intersection of condensation water tank 16, first on the cabinet 1
Pipe heat exchanger 17, second intersects pipe heat exchanger 18, compressor 19, refrigerant circulation pump 20 and condensate water circulatory pump 21, described
First intersection pipe heat exchanger 17, which is provided with, not to be connected to but adjacent the first refrigerant channel 22 and waste liquid runner 23 mutually, and described second
Intersect pipe heat exchanger 18 and be provided with and be not connected to but adjacent the second refrigerant channel 24 and condensed water runner 25 mutually, described first is cold
Matchmaker's runner 22, compressor 19, refrigerant circulation pump 24 head and the tail of the 20, second refrigerant channel are sequentially communicated and internal filling flowing have it is cold
Matchmaker, the condensation water tank 16, condensate water circulatory pump 21, condensed water runner 25 and 15 head and the tail of condensate liquid runner are sequentially communicated and inside
Filling flowing has condensed water, and the outlet of the waste liquid runner 23 is connected to the Waste liquid atomization entrance 8, the waste liquid runner 23
Entrance is in communication with the outside.
In machine starting, axial flow blower 7 starts, so the gas-liquid inner treatment chamber of entire closed loop can generate circulation
Air-flow, arrow direction is the flow direction of air-flow in Fig. 2, and the waste water after plating heats in the first intersection pipe heat exchanger 17
Enter in spray chamber 2 from Waste liquid atomization entrance 8 afterwards, then the waste liquid after high-temperature atomizing is solid by first in waste liquid separation chamber 3
Liquid/gas separator 9, the first solid-liquid separator 9 intercept waste residue therein, and remaining vapor passes through 10 He of gas heat exchanger
It is discharged and is recycled by water purification water outlet 12 at water purification after condenser 13 is cooling, it is above just to complete what waste residue was separated with condensing recovery water
Process, process is simple, direct, and energy consumption is few, and in addition the gas-liquid process chamber configurations of closed loop are simple, and occupied area is small, manufacture and use
It is at low cost.
In the present embodiment, the water purification recovery room 4 is provided with end to end two, two water purification recovery rooms 4
Be arranged side by side setting, and the lower end of two water purification recovery rooms 4 is provided with water purification collecting chamber 26, two water purification recovery rooms 4
Between be provided with to the water purification collecting chamber 26 extend partition 27, the bottom of the partition 27 and the water purification collecting chamber 26 are close
Envelope connection, is provided with airflow-reversing mouth 28 between the side of the partition 27 and the water purification collecting chamber 26.
First solid-liquid separator 9 and the second solid-liquid separator 14 are several wave-shape boards 29 arranged in parallel, institute
The solid recoverer 30 that wave-shape board 29 is provided with protrusion is stated, when the waste liquid of atomization is by the intercepted filtering of solid recoverer 30, knot
Structure is simple, and filter effect is good, and the position of first solid-liquid separator 9 and the second solid-liquid separator 14 is corresponded on the cabinet 1
It is provided with maintenance door, when the first solid-liquid separator 9 and the second solid-liquid separator 14 reach the filtering limit, replacement the first solid-liquid point
From device 9 and the second solid-liquid separator 14, wave-shape board 29 can also be porous plate, and surface has the micropore knot of absorption molecule
Structure, adsorption effect is good, adsorbs the more efficient of waste residue.
A liquid separatnig plate 31 is also equipped between the spray chamber 2, waste liquid separation chamber 3, the waste water flowing after making atomization
More disperse, make full use of the width of the first solid-liquid separator 9, avoids the first solid-liquid separator 9 using unevenness.
The exhausted bath box 32 being connected to the entrance of the waste liquid runner 23, the waste liquid separation are also equipped on the cabinet 1
Room 3 is provided with the devil liquor recovery pipe 33 being connected to the exhausted bath box 32, is equipped with water pump in the exhausted bath box 32, when there is part mist
Waste liquid after change directly passes back into exhausted bath box 32 after condensing in advance, be pumped into again by water pump in the first intersection pipe heat exchanger 17 into
The new circular treatment of row.
Main operational principle, process and effect of the invention are as follows:
The principle freezed using refrigerating field, present principles are directly to intersect pipe type heat transfer using air conditioning field principle, first
It is the heat exchanger of air-conditioner outdoor unit that device 17 is corresponding, and it is the condensation of air conditioner indoor unit that the second intersection pipe heat exchanger 18 is corresponding
Device, corresponding refrigerant is the refrigerants such as the freon that air conditioner uses, and not only heated but also freezed under unit quantity of electricity, and made full use of electric energy,
Energy consumption is than high；In addition the gas-liquid of closed loop handles circulating internal air to handle the waste water after atomization, by the waste water after atomization
In waste residue and water purification separate, utilization, detailed process is separately recovered in water purification and waste residue are as follows:
In machine starting, axial flow blower 7,21 starting of compressor 2, refrigerant circulation pump 20 and condensate water circulatory pump are entirely closed
The gas-liquid inner treatment chamber of ring can generate the air-flow of circulation, and arrow direction is the flow direction of air-flow in Fig. 2, useless after plating
Water flows into first through waste liquid runner 23 and intersects in pipe heat exchanger 17, and the refrigerant of high-temperature gas intersects pipe type heat transfer first at this time
Device 17 generates heat exchange through the waste water of the first refrigerant channel 22 and low temperature, and waste water is warmed heating, waste water be heated after from waste liquid
Atomization entrance 8 is atomized into gaseous state and enters in spray chamber 2, and then the waste liquid after high-temperature atomizing is by first in waste liquid separation chamber 3
Solid-liquid separator 9, the first solid-liquid separator 9 intercept waste residue therein, and remaining high-temperature vapor passes through gas converting heat
It is discharged and is recycled by water purification water outlet 12 at water purification after device 10 and condenser 13 are cooling, gaseous refrigerant is changed by the first intersection tubular type
The refrigerant that liquid is compressed into compressor 2 is flowed into after first refrigerant channel 22 of hot device 17, the refrigerant of liquid flows into second and hands over
The second refrigerant channel 24 in branch pipe type heat exchanger 18, the high-temperature condensation water in condensation water tank 16 are pumped into through condensate water circulatory pump 21
Second intersects in the condensed water runner 25 in pipe heat exchanger 18, and the refrigerant of liquid is through the second refrigerant channel 24 and condensed water runner
High-temperature condensation water in 25 generates heat exchange, and high-temperature condensation water becomes low temperature cold condensate, and low temperature cold condensate is through condensate liquid runner 15
Heat exchange is generated with high-temperature vapor, the water purification that high-temperature vapor is condensed into liquid is recycled, remaining cryogenic gas passes through gas
The cold air runner 11 of body heat exchanger 10 is tentatively cooled down the high-temperature vapor in inflow gas Heat Room 5, finally through being subcooled
Condensed water after the heating of lime set runner 15, which is passed back into again in condensation water tank 16, to be started to recycle next time, last cryogenic gas warp
Circulating cold air room 6 flows into spray chamber 2, and the refrigerant of liquid is through the condensation aquatic products in the second refrigerant channel 24 and condensed water runner 25
Heat exchange, the refrigerant of liquid be warmed into high-temperature gas into first intersection pipe heat exchanger 17 in start to recycle next time,
Entire waste water atomization process, the process of separation take full advantage of the electric energy of compressor refrigeration, and energy-saving effect is good, and due to
Gas-liquid process chamber is enclosed environment, and gas caused by waste liquid hardly leaks, and will not pollute air, environmental-friendly, waste water
Treatment process is simple, direct, and energy consumption is few.
The above described is only a preferred embodiment of the present invention, be not intended to limit the present invention in any form, it is all
It is any simple modification, equivalent change and modification to the above embodiments according to the technical essence of the invention, still falls within
In the range of technical solution of the present invention.
Claims (5)
1. a kind of water process evaporates reclamation set, including cabinet (1), it is characterised in that it is S-shaped to be equipped with one in the cabinet (1)
The gas-liquid process chamber of closed loop, the gas-liquid process chamber are provided with spray chamber (2), waste liquid separation chamber (3), gas that head and the tail are sequentially communicated
The upper end of body Heat Room (5) and water purification recovery room (4), the waste liquid separation chamber (3) and water purification recovery room (4) is additionally provided with cold air
The upper end of circular chamber (6), the spray chamber (2) is equipped with axial flow blower (7) and Waste liquid atomization entrance (8), the Waste liquid atomization
Entrance (8) is arranged at the air outlet of the axial flow blower (7), is equipped with the first solid-liquid in the middle part of the waste liquid separation chamber (3)
Separator (9), the gas converting heat room (5) is interior to be equipped with a gas heat exchanger (10), and the gas heat exchanger (10) is provided with
Intersect and mutually the hot gas runner of connection and cold air runner (11), the hot gas runner are not connected to the gas converting heat room (5), institute
It states cold air runner to be connected to the circulating cold air room (6), outlet and the axial flow blower (7) of the circulating cold air room (6)
Air inlet connection, the bottom of the water purification recovery room (4) are provided with water purification water outlet (12), in the water purification recovery room (4)
Condenser (13) and the second solid-liquid separator (14) be installed, the condenser (13) is provided with several and is alternatively arranged and mutually
The condensate liquid runner (15) of connection is also equipped with condensation water tank (16) on the cabinet (1), first intersects pipe heat exchanger
(17), second intersects pipe heat exchanger (18), compressor (19), refrigerant circulation pump (20) and condensate water circulatory pump (21), described
First, which intersects pipe heat exchanger (17), is provided with and is not connected to but adjacent the first refrigerant channel (22) and waste liquid runner (23) mutually, institute
It states the second intersection pipe heat exchanger (18) and is provided with and be not connected to but adjacent the second refrigerant channel (24) and condensed water runner mutually
(25), first refrigerant channel (22), compressor (19), refrigerant circulation pump (20), the second refrigerant channel (24) head and the tail successively
Connection and internal filling flowing have a refrigerant, the condensation water tank (16), condensate water circulatory pump (21), condensed water runner (25) and cold
Lime set runner (15) is sequentially communicated from beginning to end and internal filling flowing has condensed water, and the outlet of the waste liquid runner (23) is given up with described
Liquid mist dissolves into mouth (8) connection, and the entrance of the waste liquid runner (23) is in communication with the outside.
2. water process according to claim 1 evaporates reclamation set, it is characterised in that the water purification recovery room (4) is provided with
End to end two, two water purification recovery rooms (4) are arranged side by side setting, the lower end of two water purification recovery rooms (4)
It is provided with water purification collecting chamber (26), is provided between two water purification recovery rooms (4) to the water purification collecting chamber (26) and is extended
Partition (27), the bottom of the partition (27) and the water purification collecting chamber (26) be tightly connected, the side of the partition (27)
Airflow-reversing mouth (28) are provided between the water purification collecting chamber (26).
3. water process according to claim 1 evaporates reclamation set, it is characterised in that first solid-liquid separator (9) and
Second solid-liquid separator (14) is several wave-shape boards arranged in parallel (29), and the wave-shape board (29) is provided with consolidating for protrusion
Body recoverer (30).
4. water process according to claim 1 evaporates reclamation set, it is characterised in that the spray chamber (2), waste liquid separation
A liquid separatnig plate (31) are also equipped between room (3).
5. water process according to claim 1 evaporates reclamation set, it is characterised in that be also equipped on the cabinet (1) with
The exhausted bath box (32) of the entrance connection of the waste liquid runner (23), the waste liquid separation chamber (3) are provided with and the exhausted bath box
(32) the devil liquor recovery pipe (33) being connected to, the exhausted bath box (32) is interior to be equipped with water pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910161060.4A CN109734147A (en) | 2019-03-04 | 2019-03-04 | A kind of water process evaporation reclamation set |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910161060.4A CN109734147A (en) | 2019-03-04 | 2019-03-04 | A kind of water process evaporation reclamation set |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109734147A true CN109734147A (en) | 2019-05-10 |
Family
ID=66369201
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910161060.4A Pending CN109734147A (en) | 2019-03-04 | 2019-03-04 | A kind of water process evaporation reclamation set |
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| Country | Link |
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| CN (1) | CN109734147A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110130437A (en) * | 2019-06-20 | 2019-08-16 | 上海共杰机械有限公司 | Water environment-friendly cycle closestool |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20130058839A (en) * | 2011-11-28 | 2013-06-05 | 장동현 | Apparatus for treatment wastewater |
| CN204384910U (en) * | 2014-12-26 | 2015-06-10 | 广州熵利节能技术有限公司 | A kind of heat pump waste disposal plant |
| CN105344119A (en) * | 2015-11-30 | 2016-02-24 | 浙江奇彩环境科技有限公司 | Low-temperature spray evaporation waste water treatment device and waste water treatment method |
| CN105819531A (en) * | 2016-05-12 | 2016-08-03 | 上海朴是环境科技有限公司 | Energy-saving heat pump type intermediate-temperature spray evaporation system |
| CN209974347U (en) * | 2019-03-04 | 2020-01-21 | 中山地通光纤科技有限公司 | Water treatment evaporation recycling device |
-
2019
- 2019-03-04 CN CN201910161060.4A patent/CN109734147A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20130058839A (en) * | 2011-11-28 | 2013-06-05 | 장동현 | Apparatus for treatment wastewater |
| CN204384910U (en) * | 2014-12-26 | 2015-06-10 | 广州熵利节能技术有限公司 | A kind of heat pump waste disposal plant |
| CN105344119A (en) * | 2015-11-30 | 2016-02-24 | 浙江奇彩环境科技有限公司 | Low-temperature spray evaporation waste water treatment device and waste water treatment method |
| CN105819531A (en) * | 2016-05-12 | 2016-08-03 | 上海朴是环境科技有限公司 | Energy-saving heat pump type intermediate-temperature spray evaporation system |
| CN209974347U (en) * | 2019-03-04 | 2020-01-21 | 中山地通光纤科技有限公司 | Water treatment evaporation recycling device |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110130437A (en) * | 2019-06-20 | 2019-08-16 | 上海共杰机械有限公司 | Water environment-friendly cycle closestool |
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