CN206995900U - A kind of reduction device for PCB waste liquids - Google Patents
A kind of reduction device for PCB waste liquids Download PDFInfo
- Publication number
- CN206995900U CN206995900U CN201720837311.2U CN201720837311U CN206995900U CN 206995900 U CN206995900 U CN 206995900U CN 201720837311 U CN201720837311 U CN 201720837311U CN 206995900 U CN206995900 U CN 206995900U
- Authority
- CN
- China
- Prior art keywords
- distillation still
- cold
- reduction device
- communicating pipe
- waste liquids
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
It the utility model is related to a kind of reduction device for PCB waste liquids, including distillation still, the liquid feeding end of the distillation still is connected by communicating pipe with the outlet end of waste liquid pool, the top of the distillation still is provided with steam (vapor) outlet, the steam (vapor) outlet is connected by communicating pipe with the admission end of water leg, vacuum orifice is additionally provided with the top of the distillation still, and it is connected with vacuum pumping pump, also include cold and hot compressor, the thermal source output end of the cold and hot compressor is connected in distillation still, circulating-heating distillation still is set, the cooling output end of the cold and hot compressor was connected on the communicating pipe to connect with water leg, cool down the steam in the communicating pipe to connect with water leg.The utility model can be evaporated the waste water in wastewater disposal basin using the principle of evaporation by the equipment, so as to reduce the proportion of waste water, reach the purpose for reducing cost recovery.
Description
Technical field
It the utility model is related to a kind of reduction device, more particularly to a kind of reduction device for PCB waste liquids.
Background technology
Now for caused waste liquid after PCB productions, handled using third party's processing mechanism, and handle these
Waste liquid needs to pay certain expense, and the expense is paid according to the form of weight, and wherein big for PCB waste liquids
Partial weight then comes from waste water, and the proportion shared by other metal impurities is fewer for water, thus can
Result in the need for paying larger expense, so as to increase the cost of enterprise, the outdoor natural evaporation outfit of use of most original is retractable
Formula awning, but extremely inefficient, 100 tpds of amounts less than 1 ton, daily waste liquid amount are all at least more than 20 tons, can not be met
Demand.It is another have attempt it is outdoor directly heat distillation, but after heating waste liquid can produce at high temperature dangerous combustion (such as sulfur dioxide,
Chlorine, carbon monoxide etc.) pollution environment cause to forbid.
In view of it is above-mentioned the defects of, the design people, be actively subject to research and innovation, to found a kind of being used for for new structure
The reduction device of PCB waste liquids, make it with more the value in industry.
Utility model content
In order to solve the above technical problems, the purpose of this utility model is to provide a kind of reduction device for PCB waste liquids.
To achieve the above object, the utility model adopts the following technical scheme that：
A kind of reduction device for PCB waste liquids, including distillation still, the liquid feeding end of the distillation still by communicating pipe and give up
The outlet end of liquid pool is connected, and the top of the distillation still is provided with steam (vapor) outlet, and the steam (vapor) outlet passes through communicating pipe and collection
The admission end of tank is connected, and vacuum orifice is additionally provided with the top of the distillation still, and is connected with vacuum pumping pump, in addition to
Cold and hot compressor, the thermal source output end of the cold and hot compressor are connected in distillation still, and circulating-heating distillation still is set, described cold
The cooling output end of thermocompressor was connected on the communicating pipe to connect with water leg, was cooled down in the communicating pipe to connect with water leg
Steam.
Further, described a kind of reduction device for PCB waste liquids, wherein, the distillation still is double-decker
Distillation still, and be engaged in interlayer provided with recirculated water with the thermal source of cold and hot compressor.
Further, described a kind of reduction device for PCB waste liquids, wherein, the distillation still and waste liquid pool phase
Electronic control valve is provided with the communicating pipe of connection.
Further, described a kind of reduction device for PCB waste liquids, wherein, set on the top of the distillation still
Cleaning interface is equipped with, the cleaning interface is provided with 3, is distributed in equilateral triangle on the outer end at the top of distillation still, the cleaning
One end of interface is connected by communicating pipe with liquid supplying device, and the other end of the cleaning interface is injected through the top of distillation still
Into the inner chamber of distillation still, bulb is provided with the other end of the cleaning interface, delivery port is offered on the bulb, is rotated
Endoporus is offered on spray head, the rotary spray headgear is connected on bulb, and does rotary setting by axle center of bulb, along described
The periphery of rotary spray head offers some apopores, and is connected with the delivery port of cleaning interface and bulb, the distillation still
Bottom on offer outlet, and be connected by communicating pipe with rubbish collecting device.
A kind of further again, described reduction device for PCB waste liquids, wherein, stretch into the institute of distillation still inner chamber
The length of cleaning interface is stated at 20 millimeters to 35 millimeters.
A kind of further again, described reduction device for PCB waste liquids, wherein, the apopore is in the shape of a spiral
It is distributed on rotary spray head.
A kind of further again, described reduction device for PCB waste liquids, wherein, the water leg includes tank
Body, is provided with baffle plate in the inner chamber of the water trough body, and the baffle plate is located at the steam outlet of water trough body, and by tank
Body is divided into left chamber body and right chamber body, and the area of the left chamber body is more than the area of right chamber body, in the inner chamber of the water trough body
Some pieces of cold plates are additionally provided with, are set in parallel between the cold plate and cold plate, and are provided with spacing between the two, it is described
Cold plate is inclined to be arranged in the inner chamber of water trough body, and the low side of the cold plate is arranged in left chamber body, high-end setting
In right chamber body, the cold plate positioned at least significant end is set in the upper end of baffle plate, and is provided with gap, the water trough body between the two
On offer apopore.
A kind of further again, described reduction device for PCB waste liquids, wherein, on the surface of the cold plate
Guide groove is offered, guide groove is set towards the bottom surface of water trough body.
A kind of further again, described reduction device for PCB waste liquids, wherein, the guide groove is set in grid
Put on cold plate.
A kind of further again, described reduction device for PCB waste liquids, wherein, the cold and hot compressor it is cold
But output end is also connected with water leg.
By such scheme, the utility model at least has advantages below：
The utility model is that the water content in PCB waste liquids is effective by being cooperated between distillation still and cold and hot compressor
Reduction, so as to reduce the weight of PCB waste liquids, effectively reduce its extra payment cost.And the utility model is also by cold
Cooperation between thermocompressor and water leg can be such that the water vapour at distillation still distillation is quickly dropped by cold and hot compressor
Low temperature, so that gas will not discharge outdoor, is collected in the form of flowing water, effectively improves its working environment.
Described above is only the general introduction of technical solutions of the utility model, in order to better understand skill of the present utility model
Art means, and being practiced according to the content of specification, with preferred embodiment of the present utility model and coordinate accompanying drawing detailed below
Describe in detail bright as after.
Brief description of the drawings
, below will be to required use in embodiment in order to illustrate more clearly of the technical scheme of the utility model embodiment
Accompanying drawing be briefly described, it will be appreciated that the following drawings illustrate only some embodiments of the present utility model, therefore should not be by
Regard the restriction to scope as, for those of ordinary skill in the art, on the premise of not paying creative work, may be used also
To obtain other related accompanying drawings according to these accompanying drawings.
Fig. 1 is structural representation of the present utility model；
Fig. 2 is the structural representation of distillation still of the present utility model；
Fig. 3 is the structural representation of water leg of the present utility model.
Embodiment
With reference to the accompanying drawings and examples, specific embodiment of the present utility model is described in further detail.Below
Embodiment is used to illustrate the utility model, but is not limited to the scope of the utility model.
In order that those skilled in the art more fully understand the utility model, it is real below in conjunction with the utility model
Accompanying drawing in example is applied, the technical scheme in the embodiment of the utility model is clearly and completely described, it is clear that described reality
It is only the utility model part of the embodiment to apply example, rather than whole embodiments.Described in usual accompanying drawing here and show
The component of the utility model embodiment gone out can be configured to arrange and design with a variety of.Therefore, below in accompanying drawing
The detailed description of the embodiment of the present utility model of middle offer is not intended to limit claimed the scope of the utility model, and
It is to be merely representative of selected embodiment of the present utility model.Based on embodiment of the present utility model, those skilled in the art are not having
The every other embodiment obtained on the premise of making creative work, belong to the scope of the utility model protection.
Embodiment
As shown in figure 1, a kind of reduction device for PCB waste liquids, including distillation still 1, the liquid feeding end of the distillation still 1 lead to
The outlet end that communicating pipe 3 is spent with waste liquid pool 2 is connected, and the top of the distillation still 1 is provided with steam (vapor) outlet, the steam (vapor) outlet
It is connected by communicating pipe 3 with the admission end of water leg 4, vacuum orifice is additionally provided with the top of the distillation still 1, and with taking out
Vavuum pump 5 is connected, in addition to cold and hot compressor 6, the thermal source output end of the cold and hot compressor 6 are connected in distillation still 1, circulates
Heating distillation still 1 is set, and the cooling output end of the cold and hot compressor 6 was connected on the communicating pipe 3 to connect with water leg 4, cold
But the steam in communicating pipe 3 to connect with water leg 4.Made by the cooperation between distillation still 1 and cold and hot compressor 6 in distillation still
Waste liquid in 1 is discharged the water in waste liquid by way of heating by way of gas, is effectively reduced the weight of waste liquid,
So as to reduce its cost.
Distillation still 1 described in the utility model be double-decker distillation still 1, and in interlayer be provided with recirculated water with it is cold and hot
Compressor 6 is engaged, and distillation still 1 is designed into the structure in double-decker, i.e. inner barrel and outer barrel, and is used as matchmaker using water between the two
It is situated between and heating water is carried out by cold and hot compressor 6, so that the temperature of interior bucket remains at the temperature specified, it is ensured that distillation still
1 evaporation effect.
Electronic control valve 7, institute are provided with the communicating pipe 3 that distillation still 1 described in the utility model is connected with waste liquid pool 2
State electronic control valve 7 with PLC control devices to be connected, be responsible for controlling all working flow of the equipment, the PLC control devices are not existing
There is technology no longer to do any detailed description.
Embodiment one
On the basis of embodiment, as shown in Fig. 2 cleaning interface 11 is provided with the top of the distillation still 1, it is described
Clean interface 11 and be provided with 3, be distributed in equilateral triangle on the outer end at the top of distillation still 1, one end of the cleaning interface 11 leads to
Cross and be connected with liquid supplying device 12 communicating pipe 3, the other end of the cleaning interface 11 is incident upon distillation through the top of distillation still 1
In the inner chamber of kettle 1, bulb 13 is provided with the other end of the cleaning interface 11, delivery port is offered on the bulb 13, revolves
Turn to offer endoporus on spray head 14, the rotary spray first 14 is socketed on bulb 13, and is done and rotated for axle center with bulb 13
Set, some apopores are offered along the periphery of the rotary spray first 14, and with cleaning the delivery port of interface 11 and bulb 13
It is connected, outlet is offered on the bottom of the distillation still 1, and be connected with rubbish collecting device 15 by communicating pipe.
Embodiment one can make the inwall of distillation still 1 handle the state of cleaning all the time simultaneously, prevent miscellaneous in waste liquid waste liquid
Confrontation inwall impacts.
And the length of the cleaning interface 11 of the inner chamber of distillation still 1 is stretched into embodiment one at 20 millimeters to 35 millimeters, and
And the apopore is distributed on rotary spray first 14 in the shape of a spiral, it can be ensured that cleaning interface, which is cleaned in distillation still 1, to be owned
Position.
Embodiment two
On the basis of embodiment and/or embodiment one, as shown in figure 3, include water trough body 41 in the water leg 4,
Baffle plate 42 is provided with the inner chamber of the water trough body 41, the baffle plate 42 is located at the steam (vapor) outlet 2 of water trough body 41, and will
Water trough body 41 is divided into left chamber body 43 and right chamber body 44, and the area of the left chamber body 43 is more than the area of right chamber body 44, the water
Some pieces of cold plates 45 are additionally provided with the inner chamber of groove body 41, are set in parallel between the cold plate 45 and cold plate 45,
And spacing is provided between the two, the cold plate 45 is inclined to be arranged in the inner chamber of water trough body 41, the cold plate 45
Low side be arranged in left chamber body 43, high-end to be arranged in right chamber body 44, the cold plate 45 positioned at least significant end is in the upper of baffle plate 42
End is set, and is provided with gap between the two, and apopore 46 is offered in the water trough body 41.
And the gas that can be discharged distillation still 1 by the design in water leg in embodiment two quickly condenses and is in
Water, and collect.
Embodiment three
On the basis of embodiment two, in the case where not changing the structure of water leg, it will be opened up on the surface of the cold plate 45
There is guide groove 47, guide groove is set towards the bottom surface of water trough body 41.The guide groove 47 is arranged on cold plate 45 in grid,
The cooling output end of the cold and hot compressor 6 is also connected with water leg 4 simultaneously.By opening up guide groove and by cold and hot compressor
Add in water leg, the further cooling treatment accelerated to steam.
Operation principle of the present utility model is as follows：
During specific works, by PLC control devices, the gas in the inner chamber of distillation still 1 is vacuumized by place by vacuum pumping pump 5
Reason, then PLC control devices control electronic control valve 7, makes waste liquid from waste liquid pool 2 in input value distillation still 1, and then PLC is controlled
Device processed is controlled cold and hot compressor 6, and distillation still 1 is heated by cold and hot compressor 6, makes the temperature in distillation still 1
Degree lifting, after waste liquid is heated into certain temperature, wherein, the water in waste liquid is evaporated by high temperature by being expelled to collection communicating pipe
In tank, by cold and hot compressor again by PLC control devices during towards water leg, it is that steam exists to start cold air
After entering in communicating pipe, timely it can be in contact with cold air so as to reduce the temperature of steam, after entering in water leg, then
It can quickly be condensed after being met with the cold plate in water leg, so that steam turns to water, collected and post-process by water leg.
The utility model is that the water content in PCB waste liquids is effective by being cooperated between distillation still and cold and hot compressor
Reduction, so as to reduce the weight of PCB waste liquids, effectively reduce its extra payment cost.And the utility model is also by cold
Cooperation between thermocompressor and water leg can be such that the water vapour at distillation still distillation is quickly dropped by cold and hot compressor
Low temperature, so that gas will not discharge outdoor, is collected in the form of flowing water, effectively improves its working environment.
Described above is only preferred embodiment of the present utility model, is not limited to the utility model, it is noted that
For those skilled in the art, on the premise of the utility model technical principle is not departed from, can also do
Go out some improvement and modification, these improvement and modification also should be regarded as the scope of protection of the utility model.
Claims (10)
- A kind of 1. reduction device for PCB waste liquids, it is characterised in that：Including distillation still (1), the feed liquor of the distillation still (1) End is connected by communicating pipe (3) with the outlet end of waste liquid pool (2), and the top of the distillation still (1) is provided with steam (vapor) outlet, institute State steam (vapor) outlet by communicating pipe (3) with the admission end of water leg (4) to be connected, also set up on the top of the distillation still (1) There is vacuum orifice, and be connected with vacuum pumping pump (5), in addition to cold and hot compressor (6), the thermal source of the cold and hot compressor (6) are defeated Go out end to be connected in distillation still (1), circulating-heating distillation still (1) is set, the cooling output end connection of the cold and hot compressor (6) To the communicating pipe (3) to connect with water leg (4), the steam in the communicating pipe (3) to connect with water leg (4) is cooled down.
- A kind of 2. reduction device for PCB waste liquids according to claim 1, it is characterised in that：The distillation still (1) is The distillation still (1) of double-decker, and be engaged in interlayer provided with recirculated water with the thermal source of cold and hot compressor (6).
- A kind of 3. reduction device for PCB waste liquids according to claim 1, it is characterised in that：The distillation still (1) with Electronic control valve (7) is provided with the communicating pipe (3) that waste liquid pool (2) is connected.
- A kind of 4. reduction device for PCB waste liquids as claimed in any of claims 1 to 3, it is characterised in that：Institute State and cleaning interface (11) is provided with the top of distillation still (1), the cleaning interface (11) is provided with 3, is distributed in equilateral triangle On the outer end at the top of distillation still (1), one end of the cleaning interface (11) is connected by communicating pipe (3) with liquid supplying device (12) Logical, the other end of the cleaning interface (11) passes through to be incident upon in the inner chamber of distillation still (1) at the top of distillation still (1), described clear Wash on the other end of interface (11) and be provided with bulb (13), delivery port, rotary spray head (14) are offered on the bulb (13) On offer endoporus, the rotary spray head (14) is socketed on bulb (13), and with bulb (13) be axle center do rotary setting, Some apopores are offered along the periphery of the rotary spray head (14), and with cleaning the delivery port of interface (11) and bulb (13) It is connected, outlet is offered on the bottom of the distillation still (1), and be connected with rubbish collecting device (15) by communicating pipe It is logical.
- A kind of 5. reduction device for PCB waste liquids according to claim 4, it is characterised in that：Stretch into distillation still (1) The length of the cleaning interface (11) of chamber is at 20 millimeters to 35 millimeters.
- A kind of 6. reduction device for PCB waste liquids according to claim 4, it is characterised in that：The apopore is in spiral shell Rotation shape is distributed on rotary spray head (14).
- A kind of 7. reduction device for PCB waste liquids as claimed in any of claims 1 to 3, it is characterised in that：Institute Stating water leg (4) includes water trough body (41), and baffle plate (42), the baffle plate are provided with the inner chamber of the water trough body (41) (42) it is located at the steam outlet of water trough body (41), and water trough body (41) is divided into left chamber body (43) and right chamber body (44), The area of the left chamber body (43) is more than the area of right chamber body (44), is additionally provided with the inner chamber of the water trough body (41) some Block cold plate (45), it is set in parallel between the cold plate (45) and cold plate (45), and is provided with spacing between the two, it is described Cold plate (45) is inclined to be arranged in the inner chamber of water trough body (41), and the low side of the cold plate (45) is arranged on left chamber body (43) high-end to be arranged in right chamber body (44) in, the cold plate (45) positioned at least significant end is set in the upper end of baffle plate (42), and two Gap is provided between person, apopore (46) is offered on the water trough body (41).
- A kind of 8. reduction device for PCB waste liquids according to claim 7, it is characterised in that：The cold plate (45) Surface on offer guide groove (47), guide groove is set towards the bottom surface of water trough body (41).
- A kind of 9. reduction device for PCB waste liquids according to claim 8, it is characterised in that：The guide groove (47) It is arranged in grid on cold plate (45).
- A kind of 10. reduction device for PCB waste liquids according to claim 1, it is characterised in that：The cold and hot compressor (6) cooling output end is also connected with water leg (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720837311.2U CN206995900U (en) | 2017-07-11 | 2017-07-11 | A kind of reduction device for PCB waste liquids |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720837311.2U CN206995900U (en) | 2017-07-11 | 2017-07-11 | A kind of reduction device for PCB waste liquids |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206995900U true CN206995900U (en) | 2018-02-13 |
Family
ID=61453906
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720837311.2U Active CN206995900U (en) | 2017-07-11 | 2017-07-11 | A kind of reduction device for PCB waste liquids |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206995900U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107158732A (en) * | 2017-07-11 | 2017-09-15 | 苏州卓融新能源科技有限公司 | A kind of reduction device for PCB waste liquids |
-
2017
- 2017-07-11 CN CN201720837311.2U patent/CN206995900U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107158732A (en) * | 2017-07-11 | 2017-09-15 | 苏州卓融新能源科技有限公司 | A kind of reduction device for PCB waste liquids |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108002621A (en) | A kind of vaporation-type Industrial Waste Water Treatments retracting device | |
| CN209242698U (en) | A kind of equipment recycling titanium tetrachloride from chlorination mud | |
| CN107473301A (en) | A kind of desulfurization wastewater low-temperature evaporation processing system | |
| CN206995900U (en) | A kind of reduction device for PCB waste liquids | |
| CN109626466A (en) | A kind of high temperature sewage treatment and distilled water preparation system and its control method | |
| CN110624338B (en) | Metallurgical waste gas recycles green treatment facility | |
| CN204730293U (en) | A kind of fume purifier of fume and smoke exhaust ventilator | |
| CN206127267U (en) | Distillation plant of making wine usefulness | |
| CN107158732A (en) | A kind of reduction device for PCB waste liquids | |
| CN205235573U (en) | Waste water cyclic utilization system is handled to intermediate frequency furnace flue gas | |
| CN210242449U (en) | Tail gas treatment device of hot air circulation degreasing furnace | |
| CN209791203U (en) | Saturated steam's white system that disappears | |
| CN207405012U (en) | A kind of energy saving environment protection domestic sewage-treatment plant | |
| CN205690967U (en) | A kind of cleaning plant of multi-runner heat exchanging device | |
| CN108548239A (en) | A kind of spray purification device killed bacterium and reduce PM2.5 | |
| CN108862796A (en) | Industrial sewage processing unit and its working method | |
| CN204873907U (en) | Hot pressing formula distilled water machine system | |
| CN208757000U (en) | A kind of waste heat from tail gas recycling dehydration device | |
| CN210131508U (en) | Cooling device for organic waste gas treatment of circuit board | |
| CN208553532U (en) | A kind of emission-control equipment | |
| CN210302433U (en) | Evaporative condenser | |
| CN108840500A (en) | A kind of waste emulsified mixture processing method and processing device | |
| CN212610094U (en) | Energy-efficient low temperature evaporation concentration equipment | |
| CN209475626U (en) | Dangerous waste aqueous industrial high-temperature gas containing dust condenses process equipment | |
| CN213790611U (en) | Germanium concentrate calcination tail gas combination formula multistage absorption washing device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |