CN208776347U - Waste liquid enrichment facility - Google Patents
Waste liquid enrichment facility Download PDFInfo
- Publication number
- CN208776347U CN208776347U CN201821318640.7U CN201821318640U CN208776347U CN 208776347 U CN208776347 U CN 208776347U CN 201821318640 U CN201821318640 U CN 201821318640U CN 208776347 U CN208776347 U CN 208776347U
- Authority
- CN
- China
- Prior art keywords
- groove tank
- waste liquid
- tank
- condenser
- vacuum pump
- 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
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
The utility model proposes a kind of waste liquid enrichment facilities, comprising: the top of groove tank, the groove tank has exhaust outlet；Heater, the heater are located in the groove tank for heating the waste liquid in the groove tank；Condenser, the input terminal of the condenser are connected with the exhaust outlet；Water receiving tank, the water receiving tank are located at below the condenser to accept the condensate liquid dripped on the condenser, have discharge outlet on the water receiving tank；Vacuum pump, the input terminal of the vacuum pump is connected with the output end of the condenser and the output end of the vacuum pump is connected to the groove tank；Reservoir, the reservoir are connected to the groove tank.Waste liquid enrichment facility according to the present utility model will not generate gas and dissipate and overflow and lead to secondary pollution, process flow is simple and effective, rapid evaporation rapid condensation, and thickening efficiency is high using whole closing appliance.
Description
Technical field
The utility model relates to technical field of water pollution treatment, more particularly to a kind of waste liquid enrichment facility.
Background technique
At this stage, environmental protection has been established as the fundamental state policy in China in environmental law.As the waste water in environmental protection
Processing, the discharge standard of Industrial Wastewater Treatment is also more and more harsh, and existing technology for treating industrial waste water faces huge challenge, former
In some technologies, high danger wastes disposal costs bring biggish economic pressures to enterprise, as in waste liquid disposition
Key technology, waste liquid minimizing disposition become the main points paid close attention at this stage.
Nowadays in wastewater minimisation or even zero-discharge technology, evaporation concentration equipment and technique are increasingly subject to praise highly, such as MVR, more
Evaporator, film evaporation etc. are imitated, is all to reach wastewater minimisation using thermal evaporation techniques.Although there is certain actual effect,
Still occur many defects in actual motion, as the energy consumption of ton evaporated quantity of water is especially big, the easy scale effect of equipment is continuously run,
Equipment is perishable, process flow is complicated, equipment land occupation is big, evaporation efficiency is low.Even some produce pernicious gas and spill into air
In, lead to more serious secondary pollution, needs the waste gas treatment equipment of mating complexity.
Utility model content
The utility model is intended to solve at least some of the technical problems in related technologies.
For this purpose, a purpose of the utility model is to propose that a kind of waste liquid enrichment facility will not using whole closing appliance
It generates gas and dissipates and overflow and lead to secondary pollution, process flow is simple and effective, rapid evaporation rapid condensation, and thickening efficiency is high.
A kind of waste liquid enrichment facility according to the present utility model, comprising:
The top of groove tank, the groove tank has exhaust outlet；
Heater, the heater are located in the groove tank for heating the waste liquid in the groove tank；
Condenser, the input terminal of the condenser are connected with the exhaust outlet；
Water receiving tank, the water receiving tank are located to accept the condensate liquid dripped on the condenser below the condenser,
There is discharge outlet on the water receiving tank；
Vacuum pump, the input terminal of the vacuum pump is connected with the output end of the condenser and the output end of the vacuum pump
It is connected to the groove tank；
Reservoir, the reservoir are connected to the groove tank.
Advantageously, the waste liquid enrichment facility further includes demisting layer, and the demisting layer is located in the groove tank and neighbouring
The exhaust outlet.
Advantageously, the heater is located at the bottom in the groove tank and being located at the groove tank.
Advantageously, the output end of the vacuum pump protrudes into the groove tank and is located at below the heater.
Advantageously, the connecting tube of the reservoir protrudes into the groove tank and is located at below the heater.
The additional aspect and advantage of the utility model will be set forth in part in the description, partially will be from following description
In become obvious, or recognized by the practice of the utility model.
Detailed description of the invention
Fig. 1 is the schematic diagram according to the waste liquid enrichment facility of the utility model one embodiment.
Specific embodiment
The embodiments of the present invention are described below in detail, examples of the embodiments are shown in the accompanying drawings, wherein from beginning
Same or similar element or element with the same or similar functions are indicated to same or similar label eventually.Below by ginseng
The embodiment for examining attached drawing description is exemplary, it is intended to for explaining the utility model, and should not be understood as to the utility model
Limitation.
Below with reference to the accompanying drawings it is described in detail waste liquid enrichment facility according to the present utility model.
Waste liquid enrichment facility according to the present utility model, comprising: groove tank 100, heater 200, condenser 300, water receiving tank
400, vacuum pump 500, reservoir 600.
Specifically, the top of groove tank 100 has exhaust outlet 110.
Heater 200 is located in groove tank 100 for heating the waste liquid in groove tank 100.
The input terminal of condenser 300 is connected with exhaust outlet 110.
Water receiving tank 400 is located at below condenser 300 to accept the condensate liquid dripped on condenser 300, on water receiving tank 400
With discharge outlet 410.
The input terminal of vacuum pump 500 is connected with the output end of condenser 300 and the output end of vacuum pump 500 and groove tank 100
Connection.
Reservoir 600 is connected to groove tank 100.
When work, waste liquid generates steam under the heating of heater 200 in groove tank 100；Vacuum pump 500 is by gas from slot
It is sucked out in tank 100；About 50 DEG C of hot steam is condensed by condenser 300, and condensate liquid is discharged after being collected by water receiving tank；About 20-30
DEG C dry wind be discharged into groove tank by vacuum pump 500.Waste liquid enrichment facility according to the present utility model is provided dynamic by vacuum pump 500
Power makes generation negative pressure in groove tank 100 suck waste liquid from reservoir 600 automatically when waste liquid is less in groove tank 100.Using
Whole closing appliance will not generate gas and dissipate and overflow and lead to secondary pollution；Occupied area is small, and process flow is simple and effective；Rapid steaming
Rapid condensation is sent out, thickening efficiency is high.
Advantageously, the waste liquid enrichment facility further includes demisting layer 700, and demisting layer 700 is located in groove tank 100 and neighbouring
Exhaust outlet 110.Steam can remove the fogs such as droplet by demisting layer as a result,.
An example according to the present utility model, heater 200 are located at the bottom in groove tank 100 and being located at groove tank 100.Have
Sharp ground, the output end of vacuum pump 500 protrude into groove tank 100 and are located at below heater 200.As described above, about 20-30 DEG C
Dry wind is inputted in groove tank 100 by vacuum pump 500, can heat to waste liquid, saves energy consumption.Advantageously, the company of reservoir 600
Adapter tube protrudes into groove tank 100 and is located at below heater 200.
In the description of the present invention, it should be understood that term " center ", " longitudinal direction ", " transverse direction ", " length ", " width
Degree ", " thickness ", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom" "inner", "outside", " suitable
The orientation or positional relationship of the instructions such as hour hands ", " counterclockwise ", " axial direction ", " radial direction ", " circumferential direction " is orientation based on the figure
Or positional relationship, be merely for convenience of describing the present invention and simplifying the description, rather than the device of indication or suggestion meaning or
Element must have a particular orientation, be constructed and operated in a specific orientation, therefore should not be understood as the limit to the utility model
System.
In addition, term " first ", " second " are used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance
Or implicitly indicate the quantity of indicated technical characteristic.Define " first " as a result, the feature of " second " can be expressed or
Implicitly include one or more of the features.The meaning of " plurality " is two or more in the description of the present invention, remove
It is non-separately to have clearly specific restriction.
In the present invention unless specifically defined or limited otherwise, term " installation ", " connected ", " connection ", " Gu
It is fixed " etc. terms shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integral；It can be
Mechanical connection, is also possible to be electrically connected；It can be directly connected, two can also be can be indirectly connected through an intermediary
The interaction relationship of connection or two elements inside element.It for the ordinary skill in the art, can basis
Concrete condition understands the concrete meaning of above-mentioned term in the present invention.
In the present invention unless specifically defined or limited otherwise, fisrt feature is in the second feature " on " or " down "
It can be that the first and second features directly contact or the first and second features are by intermediary mediate contact.Moreover, first is special
Sign can be fisrt feature above the second feature " above ", " above " and " above " and be directly above or diagonally above the second feature, or only
Indicate that first feature horizontal height is higher than second feature.Fisrt feature under the second feature " below ", " below " and " below " can be with
It is that fisrt feature is directly under or diagonally below the second feature, or is merely representative of first feature horizontal height less than second feature.
In the description of this specification, reference term " one embodiment ", " some embodiments ", " example ", " specifically show
The description of example " or " some examples " etc. means specific features, structure, material or spy described in conjunction with this embodiment or example
Point is contained at least one embodiment or example of the utility model.In the present specification, to the schematic table of above-mentioned term
It states and is necessarily directed to identical embodiment or example.Moreover, particular features, structures, materials, or characteristics described can be with
It can be combined in any suitable manner in any one or more of the embodiments or examples.In addition, without conflicting with each other, this field
Technical staff can by the feature of different embodiments or examples described in this specification and different embodiments or examples into
Row combination and combination.
Although the embodiments of the present invention have been shown and described above, it is to be understood that above-described embodiment is
Illustratively, it should not be understood as limiting the present invention, those skilled in the art are in the scope of the utility model
It inside makes changes, modifications, substitutions and variations to the above described embodiments, each falls within the protection scope of the utility model.
Claims (5)
1. a kind of waste liquid enrichment facility characterized by comprising
The top of groove tank, the groove tank has exhaust outlet；
Heater, the heater are located in the groove tank for heating the waste liquid in the groove tank；
Condenser, the input terminal of the condenser are connected with the exhaust outlet；
Water receiving tank, the water receiving tank is located at below the condenser to accept the condensate liquid dripped on the condenser, described
There is discharge outlet on water receiving tank；
Vacuum pump, the input terminal of the vacuum pump is connected with the output end of the condenser and the output end of the vacuum pump and institute
State groove tank connection；
Reservoir, the reservoir are connected to the groove tank.
2. waste liquid enrichment facility according to claim 1, which is characterized in that further include demisting layer, the demisting layer is located at
In the groove tank and adjacent to the exhaust outlet.
3. waste liquid enrichment facility according to claim 1, which is characterized in that the heater is located in the groove tank and position
In the bottom of the groove tank.
4. waste liquid enrichment facility according to claim 3, which is characterized in that the output end of the vacuum pump protrudes into the slot
In tank and it is located at below the heater.
5. waste liquid enrichment facility according to claim 3, which is characterized in that the connecting tube of the reservoir protrudes into the slot
In tank and it is located at below the heater.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821318640.7U CN208776347U (en) | 2018-08-16 | 2018-08-16 | Waste liquid enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821318640.7U CN208776347U (en) | 2018-08-16 | 2018-08-16 | Waste liquid enrichment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208776347U true CN208776347U (en) | 2019-04-23 |
Family
ID=66157004
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821318640.7U Active CN208776347U (en) | 2018-08-16 | 2018-08-16 | Waste liquid enrichment facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208776347U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111620395A (en) * | 2020-04-14 | 2020-09-04 | 上海问鼎环保科技有限公司 | High-concentration waste liquid evaporator and waste liquid treatment method thereof |
-
2018
- 2018-08-16 CN CN201821318640.7U patent/CN208776347U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111620395A (en) * | 2020-04-14 | 2020-09-04 | 上海问鼎环保科技有限公司 | High-concentration waste liquid evaporator and waste liquid treatment method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105000612B (en) | Mechanical vapor recompression system of concentrated organic waste water and method | |
| CN207391049U (en) | A kind of evaporation and concentration processing unit of waste water/waste liquid | |
| CN103127736A (en) | Evaporation and concentration device utilizing heat pump technique | |
| CN206771805U (en) | A kind of eliminating white smoke type open absorption heat pump system for industrial waste gas waste heat recovery | |
| CN102001718B (en) | Low-pressure water-saving efficient water distiller | |
| CN206494738U (en) | Wastewater treatment equipment | |
| CN208776347U (en) | Waste liquid enrichment facility | |
| CN107572625A (en) | The evaporation and concentration processing unit and processing method of a kind of waste water/waste liquid | |
| CN106477847A (en) | A kind of Integral sludge filter pressing anhydration system | |
| CN206071788U (en) | A kind of cooling tower backwater TRT | |
| CN208097695U (en) | A kind of energy-saving and environment-friendly emission-control equipment | |
| CN204261368U (en) | A kind of low-boiling-point substance reclaimer | |
| CN207169083U (en) | A kind of ethanol device for recovering tail gas | |
| CN205672580U (en) | A kind of MVR vaporising device of movable container formula | |
| CN205897398U (en) | Cold all -in -one of evaporation | |
| CN207196985U (en) | A kind of circulating cooling-water machine | |
| CN209138027U (en) | A kind of waste heat recycling VOC condensate recovery system | |
| CN207751356U (en) | A kind of steam condenser | |
| CN202371700U (en) | Recycling device for steam condensate | |
| CN205744019U (en) | A kind of efficiently drain recovery case | |
| CN207811305U (en) | Vacuum environment desulfurization wastewater and its sludge treatment equipment | |
| CN210268258U (en) | Environment-friendly melting furnace steam recovery device | |
| CN205744020U (en) | A kind of drain recovery case | |
| CN218403720U (en) | Green sewage treatment system | |
| CN217567502U (en) | Ceramic spray drying tower tail gas treatment equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |