CN205974106U - Laboratory wastewater treatment facility - Google Patents
Laboratory wastewater treatment facility Download PDFInfo
- Publication number
- CN205974106U CN205974106U CN201620943827.0U CN201620943827U CN205974106U CN 205974106 U CN205974106 U CN 205974106U CN 201620943827 U CN201620943827 U CN 201620943827U CN 205974106 U CN205974106 U CN 205974106U
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- unit
- waste water
- fenton oxidation
- electrolysis
- spoil disposal
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Abstract
The utility model provides a laboratory wastewater treatment facility, being responsible for including waste water regulating unit, trigeminy formula reactor, many filter medium filtration unit, row's mud, wherein being provided with the immersible pump in the waste water regulating unit, dive pump outlet pipe says that it enters the mouth to connect trigeminy formula reactor, trigeminy formula reactor is established ties in proper order and is formed by the little electrolysis unit of indisputable carbon, fenton oxidation unit, flocculation and precipitation unit, is provided with respectively in the three processing unit in the trigeminy formula reactor with the medicine mouth, and the little electrolysis unit of indisputable carbon, fenton oxidation unit, flocculation and precipitation unit container bottom become back taper platform structure, and back taper platform bottom is provided with the mud pipe respectively, and row's mud is responsible for and is provided with three spinal branch pipes, connects respectively the little electrolysis unit of iron carbon, fenton oxidation unit, flocculation and precipitation unit container bottom mud pipe. The utility model has the advantages of integrated integration, high, the long service life of operation efficiency.
Description
Technical field
This utility model is related to technical field of waste water processing and in particular to a kind of Laboratory Waste Water Treatment equipment.
Background technology
Contained major pollutants property in laboratory waste water, can be divided into inorganic, organic and laboratory containing pathogenic microorganism
Waste water three major types.In Laboratory Waste Water Treatment, physical method is more effective, existing Laboratory Waste Water Treatment many using focusing on
Mode processed, carrying out Laboratory Waste Water Treatment by sewage treatment equipment is an emerging technology.
In existing sewage treatment equipment, using high-order water inlet, low level water outlet, low level water outlet can be by a upper processing unit deposition
Precipitation bring next stage processing unit into, lead to process not thorough；When in processing unit, water level is high, high-order water inlet can be impacted
To processing unit bottom, lead to deposit cannot form precipitation, thus Solid-Liquid Separation cannot be realized, lead to deposit to process not
Thoroughly；It is further also frequently with iron-carbon micro-electrolysis unit, the heavy metal substance in waste water to be carried out when to wastewater treatment
Process, generally adopt spherical ferrum carbon filler in present iron-carbon micro-electrolysis unit, easily caking is hardened due to spherical ferrum carbon filler,
Time length can not reach good treatment effect, be on the one hand unable to reach good water treatment effect, or even cannot expire
Sufficient discharge of wastewater requires, and on the other hand restricts the service life of a whole set of sewage treatment equipment.
Utility model content
The purpose of this utility model provides a kind of rational in infrastructure, Laboratory Waste Water Treatment equipment that reaction efficiency is high, utilizes
The rational layout of tri-coupling type reactor and to iron-carbon micro-electrolysis unit internal structure improve, reach quick treatment of laboratory waste water
Purpose, solve prior art in the slow-footed technical problem of Laboratory Waste Water Treatment.
For achieving the above object, this utility model be employed technical scheme comprise that：
A kind of Laboratory Waste Water Treatment equipment, including tri-coupling type reactor, described tri-coupling type reactor is by iron-carbon micro-electrolysis
Unit, Fenton oxidation unit, flocculation sediment unit are sequentially connected in series by pipeline and form, and the pipeline of unit be disposed as low
Position water inlet, high-order water outlet, the water inlet of described iron-carbon micro-electrolysis unit constitutes the entrance of tri-coupling type reactor, described flocculation sediment
The outlet of unit constitutes the outlet of tri-coupling type reactor；Wherein,
Described iron-carbon micro-electrolysis unit inside cavity is provided with support ring, and described support ring is arranged on water inlet top, institute
State and cellular ferrum carbon filler layer is provided with support ring；Ferrum carbon filler layer, described ferrum carbon filler layer are provided with described support ring
Interior vertical be provided with some cross openings, some openings of crossing become cellular arrangement, described ferrum carbon filler in ferrum carbon filler layer
Layer is obliquely installed in the lumen and is formed an angle with internal chamber wall shape；
Described iron-carbon micro-electrolysis unit, Fenton oxidation unit, the container bottom of flocculation sediment unit are respectively provided with tapered knot
Structure, and it is provided with spoil disposal arm in conical bottom, each spoil disposal arm is provided with spoil disposal valve, all spoil disposal arms all connect
It is connected on a spoil disposal supervisor.
Compared with prior art, this utility model has advantages below：
This utility model is prevented effectively from by the design of low position inflow water, high-order water outlet and is carried because of high-order water inlet, low level water outlet
The following point coming：I.e. low level water outlet can bring the precipitation of a upper processing unit deposition into next stage processing unit, leads to process
Not thorough；When in processing unit, water level is high, high-order water inlet can impact processing unit bottom, leads to deposit cannot be formed
Precipitation, thus Solid-Liquid Separation cannot be realized, leads to deposit to process not thorough；In iron-carbon micro-electrolysis unit cavity, setting props up
Pushing out ring is located at water inlet top, is conducive to the abundant CONTACT WITH FRICTION of waste water and packing layer, quickly fully removes the weight in waste water
Metallic.
In addition, this utility model by the design of tri-coupling type reactor so that in each processing unit of tri-coupling type reactor
The precipitation being formed timely is discharged it is ensured that the smoothness of spoil disposal, completeness, improves waste water treatment efficiency.
Further, due to current spherical ferrum carbon filler on the market, easily caking is hardened, affects adsorption effect during life-time service,
This utility model adopts cellular ferrum carbon filler, existing filter effect in iron-carbon micro-electrolysis unit, effectively prevent ferrum carbon again
The hardened problem of caking of packing layer, reaches the purpose increasing the service life；Using with cavity inner wall have a certain degree inclination honeybee
Nest shape structure arranges filler, on the one hand increases the contact area of waste water and filler by cellular internal structure, plays increase anti-
Answer the effect of efficiency, the through hole within honeycomb padding on the other hand tilting plays drainage so that iron-carbon micro-electrolysis list
Current in unit become rule to flow, and reduce the noise that equipment produces.
Part is embodied by further advantage of the present utility model, target and feature by description below, and part also will be passed through
Research of the present utility model and practice are understood by the person skilled in the art.
Brief description
Fig. 1 is this utility model layout drawing.
Fig. 2 is the layout drawing of this utility model embodiment 1.
Fig. 3 is cellular ferrum carbon filler structure chart in this utility model.
In figure：1：Waste water adjustment unit, 1-1：Elevator pump, 2-1：Iron-carbon micro-electrolysis unit, 2-2：Fenton oxidation unit, 2-
3：Flocculation sediment unit, 2-4：Inverted cone platform bucket, 2-5：Effusion meter, 2-6：Aeration fan, 2-7：Force (forcing) pump, 2-8：Control valve
1,2-9：Control valve 2,2-10：Cellular ferrum carbon filler layer, 2-11：Gripper shoe, 3：Multi-medium filtering unit, 4：Spoil disposal is responsible for,
4-1：Discharge pipeline A, 4-2：Discharge pipeline B, 4-3：Discharge pipeline C, 4-4：Mud valve a, 4-5：Mud valve b, 4-6：Mud valve c, 4-7：
Slush pump.
Specific embodiment
In order that the technological means of this utility model realization, creation characteristic, reached purpose and effect are more clear and are easy to
Understand, with reference to the accompanying drawings and detailed description this utility model is further elaborated.
Embodiment 1
Fig. 2 shows a kind of way of realization of the present utility model, and a kind of Laboratory Waste Water Treatment equipment is anti-including tri-coupling type
Answer device 2, tri-coupling type reactor passes through pipeline by iron-carbon micro-electrolysis unit 2-1, Fenton oxidation unit 2-2, flocculation sediment unit 2-3
It is sequentially connected in series and forms, and the pipeline of unit is disposed as low position inflow water, high-order water outlet, iron-carbon micro-electrolysis unit 2-1 enters
The mouth of a river constitutes the entrance of tri-coupling type reactor, and the outlet of flocculation sediment unit 2-3 constitutes the outlet of tri-coupling type reactor；Its
In, iron-carbon micro-electrolysis unit is internally provided with support ring 2-11 in its container, and support ring 2-11 is arranged on water inlet top, supports
Cellular ferrum carbon filler layer 2-10 is provided with ring 2-11；In ferrum carbon filler layer 2-10 vertical be provided with some cross openings,
Some cross openings become cellular arrangement in ferrum carbon filler layer, ferrum carbon filler layer 2-10 be obliquely installed in the lumen and and internal chamber wall
Shape forms an angle；
Iron-carbon micro-electrolysis unit 2-1, Fenton oxidation unit 2-2, the container bottom of flocculation sediment unit 2-3 are all provided with being set to cone
Shape structure, the effect of this pyramidal structure is easy for deposit and concentrates, and is provided with spoil disposal arm 4-1,4-2 in conical bottom respectively
And 4-3, the effect of discharge pipeline is by discharge pipeline, the precipitation depositing in processing unit to be discharged reactor, on each spoil disposal arm
It is correspondingly arranged on spoil disposal valve 4-4,4-5 and 4-6, all spoil disposal arms are connected on a spoil disposal supervisor 4.Setting mud valve
Purpose be to realize flexible spoil disposal, when in some processing unit deposition precipitation more need spoil disposal when it is only necessary to beat
The mud valve opened on this processing unit bottom discharge pipeline carries out spoil disposal, does not affect the normal process of other processing units so that giving up
Water process is more thorough, and spoil disposal is more flexible.
In technique scheme, waste water flows into from iron-carbon micro-electrolysis unit, in iron-carbon micro-electrolysis unit, to waste water
Process integrates oxidation, reduction, electro-deposition, flocculation, absorption, bridge formation, volume are swept and be co-precipitated, and has both removed part heavy metal,
Degrading microorganism, can reduce COD, colourity and ammonia nitrogen etc. again；Waste water after iron-carbon micro-electrolysis cell processing enters Fenton oxygen
Change unit and carry out oxidation processes, improve the biodegradability of waste water；Complete pollutant subsequently into flocculation sediment unit further
Remove, after through multi-medium filtering tank filter, reach discharge standard discharge.
Embodiment 2
In the present embodiment, increased waste water adjustment unit on the basis of embodiment 1, be provided with latent in waste water adjustment unit
Water pump, submersible pump outlet pipeline connects tri-coupling type reactor inlet.The purpose increasing waste water adjustment unit is that waste water pH value is entered
Row pretreatment is adjusted, and the effect adjusting pH value is in order that the treatment effect of iron-carbon micro-electrolysis unit more preferably, increases elevator pump
Effect is to adapt to the strong characteristic of laboratory waste water discontinuity, rapid starting/stopping elevator pump according to actual needs, makes technical scheme at place
During reason more efficiently, flexibly.
Embodiment 3
In the present embodiment, multi-medium filtering unit on the basis of embodiment 2, it is heavy that multi-medium filtering unit is connected to flocculation
After the unit of shallow lake, between multi-medium filtering unit and flocculation sediment unit, it is provided with force (forcing) pump, multi-medium filtering unit is provided with row
Water pipe, drain pipe is arranged on the upper end position of multi-medium filtering unit.The purpose of setting force (forcing) pump is in order that multi-medium filtering
Unit reaches the effect of pressure filtration, thus filtering more thoroughly, efficiently.
Embodiment 4
In the present embodiment, increased spoil disposal supervisor, iron-carbon micro-electrolysis unit, Fenton oxidation unit on the basis of embodiment 3
It is connected in turn on spoil disposal supervisor with the discharge pipeline of flocculation sediment unit, spoil disposal supervisor is additionally provided with slush pump, slush pump sets
Put the rear end in described flocculation sediment single-unit container discharge pipeline.Setting discharge pipeline effect be in order to realize a supervisor complete many
The spoil disposal of individual processing unit, the effect of slush pump is when deposition is more dry, not easily passs through nature sludge discharge way and discharges, then starts mud
Pumping spoil disposal, the precipitation of deposition is discharged from thorough.
Embodiment 5
In the present embodiment, increased effusion meter on the basis of embodiment 4, effusion meter is arranged on iron-carbon micro-electrolysis unit and institute
State on the pipeline connecting between wastewater equalization pond, the effect of setting effusion meter is that wastewater treatment capacity is carried out with registration, convenient reading
Related data, provides basis for later data analysis.
Embodiment 6
In the present embodiment, increased Aeration fan on the basis of embodiment 5, Aeration fan is arranged on iron-carbon micro-electrolysis unit
And Fenton oxidation unit between, two aeration opening of Aeration fan are connected to iron-carbon micro-electrolysis unit and Fenton by pipeline respectively
On oxidation unit container, the effect of Aeration fan is to iron-carbon micro-electrolysis unit and Fenton oxidation unit aeration, makes at this two
Waste water in reason unit is sufficiently mixed and obtains oxygen so that reaching maximum, sweet smell in iron-carbon micro-electrolysis unit electrolysis adsorption effect
The waste water pausing in oxidation unit is at utmost aoxidized.
Embodiment 7
In the present embodiment, the basis of embodiment 6 Aeration fan and iron-carbon micro-electrolysis unit and Fenton oxidation unit it
Between increased control valve respectively on the pipeline that connects, the effect of control valve be according to laboratory waste water pollutant situation and waste water at
Reason is actually needed, and can select khaki or close a certain control valve, make Aeration fan obtain the utilization of maximal efficiency.This enforcement
Example is most preferred embodiment of the present utility model.
Finally illustrate, above example only in order to the technical solution of the utility model to be described and unrestricted, although ginseng
According to preferred embodiment, this utility model is described in detail, it will be understood by those within the art that, can be to this
The technical scheme of utility model is modified or equivalent, the objective without deviating from technical solutions of the utility model and model
Enclose, it all should be covered in the middle of right of the present utility model.
Claims (7)
1. a kind of Laboratory Waste Water Treatment equipment is it is characterised in that include tri-coupling type reactor, described tri-coupling type reactor is by ferrum
Carbon micro-electrolysis unit, Fenton oxidation unit, flocculation sediment unit are sequentially connected in series by pipeline and form, and the pipeline of unit is equal
It is set to low position inflow water, high-order water outlet, the water inlet of described iron-carbon micro-electrolysis unit constitutes the entrance of tri-coupling type reactor, described
The outlet of flocculation sediment unit constitutes the outlet of tri-coupling type reactor；Wherein,
Described iron-carbon micro-electrolysis unit inside cavity is provided with support ring, and described support ring is arranged on water inlet top, described
Ferrum carbon filler layer is provided with pushing out ring, in described ferrum carbon filler layer vertical be provided with some cross openings, some cross openings
Become cellular arrangement in ferrum carbon filler layer, described ferrum carbon filler layer is obliquely installed in the lumen and forms a clamp with internal chamber wall
Angle；
Described iron-carbon micro-electrolysis unit, Fenton oxidation unit, the container bottom of flocculation sediment unit are respectively provided with tapered structure, and
It is provided with spoil disposal arm in conical bottom, each spoil disposal arm is provided with mud valve, all spoil disposal arms are connected to one
On individual spoil disposal supervisor.
2. Laboratory Waste Water Treatment equipment as claimed in claim 1 is it is characterised in that also including waste water adjustment unit, described useless
It is provided with immersible pump, submersible pump outlet pipeline connects tri-coupling type reactor inlet in water adjustment unit.
3. Laboratory Waste Water Treatment equipment as claimed in claim 1 or 2 is it is characterised in that also include multi-medium filtering unit, institute
State after multi-medium filtering unit is connected to flocculation sediment unit, between described multi-medium filtering unit and described flocculation sediment unit
It is provided with force (forcing) pump, described multi-medium filtering unit is provided with drain pipe, and drain pipe is arranged on the upper end of multi-medium filtering unit
Position.
4. Laboratory Waste Water Treatment equipment as claimed in claim 3 is it is characterised in that also include spoil disposal supervisor, described spoil disposal master
Slush pump is additionally provided with pipe, described slush pump is arranged on the rear end of described flocculation sediment single-unit container discharge pipeline.
5. Laboratory Waste Water Treatment equipment as claimed in claim 2 it is characterised in that described iron-carbon micro-electrolysis unit with described
It is provided with effusion meter on the pipeline connecting between waste water adjustment unit.
6. Laboratory Waste Water Treatment equipment as claimed in claim 1 or 2 it is characterised in that described iron-carbon micro-electrolysis unit with
It is provided with Aeration fan, two aeration opening of Aeration fan are connected to ferrum carbon by pipeline respectively between described Fenton oxidation unit
On light electrolysis unit and described Fenton oxidation single-unit container.
7. Laboratory Waste Water Treatment equipment as claimed in claim 6 is it is characterised in that described Aeration fan is micro- with described ferrum carbon
It is respectively arranged with control valve on the pipeline connecting between electrolysis cells and described Fenton oxidation unit.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620943827.0U CN205974106U (en) | 2016-08-25 | 2016-08-25 | Laboratory wastewater treatment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620943827.0U CN205974106U (en) | 2016-08-25 | 2016-08-25 | Laboratory wastewater treatment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205974106U true CN205974106U (en) | 2017-02-22 |
Family
ID=58035352
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620943827.0U Expired - Fee Related CN205974106U (en) | 2016-08-25 | 2016-08-25 | Laboratory wastewater treatment facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205974106U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110697982A (en) * | 2019-10-23 | 2020-01-17 | 盐城工学院 | Zero-valent iron system for in-situ removal of hydrogen sulfide in municipal sewage pipeline well and operation method thereof |
| CN110862179A (en) * | 2019-12-19 | 2020-03-06 | 锦科绿色科技(苏州)有限公司 | Water treatment system and control workstation |
| CN112390424A (en) * | 2019-08-15 | 2021-02-23 | 北京鑫宝能环境技术有限公司 | Wastewater purification treatment method and system |
-
2016
- 2016-08-25 CN CN201620943827.0U patent/CN205974106U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112390424A (en) * | 2019-08-15 | 2021-02-23 | 北京鑫宝能环境技术有限公司 | Wastewater purification treatment method and system |
| CN110697982A (en) * | 2019-10-23 | 2020-01-17 | 盐城工学院 | Zero-valent iron system for in-situ removal of hydrogen sulfide in municipal sewage pipeline well and operation method thereof |
| CN110862179A (en) * | 2019-12-19 | 2020-03-06 | 锦科绿色科技(苏州)有限公司 | Water treatment system and control workstation |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170222 Termination date: 20210825 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |