CN205953776U - Integration laboratory wastewater treatment facility - Google Patents
Integration laboratory wastewater treatment facility Download PDFInfo
- Publication number
- CN205953776U CN205953776U CN201620861105.0U CN201620861105U CN205953776U CN 205953776 U CN205953776 U CN 205953776U CN 201620861105 U CN201620861105 U CN 201620861105U CN 205953776 U CN205953776 U CN 205953776U
- Authority
- CN
- China
- Prior art keywords
- collecting pit
- lab
- treatment equipment
- sewage treatment
- flocculation basin
- 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.)
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Links
- 238000004065 wastewater treatment Methods 0.000 title abstract description 7
- 230000010354 integration Effects 0.000 title abstract 2
- 239000012528 membrane Substances 0.000 claims abstract description 39
- 238000005189 flocculation Methods 0.000 claims abstract description 32
- 230000016615 flocculation Effects 0.000 claims abstract description 32
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 12
- 230000037452 priming Effects 0.000 claims abstract description 10
- 238000006243 chemical reaction Methods 0.000 claims abstract description 7
- 230000003647 oxidation Effects 0.000 claims abstract 4
- 230000001105 regulatory effect Effects 0.000 claims description 23
- 239000010865 sewage Substances 0.000 claims description 14
- 230000014759 maintenance of location Effects 0.000 claims description 10
- 229910052799 carbon Inorganic materials 0.000 claims description 8
- 239000000523 sample Substances 0.000 claims description 8
- 238000010521 absorption reaction Methods 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 7
- 238000005276 aerator Methods 0.000 claims description 4
- 238000010992 reflux Methods 0.000 claims description 4
- 239000012530 fluid Substances 0.000 claims description 2
- 239000002351 wastewater Substances 0.000 abstract description 11
- 230000008901 benefit Effects 0.000 abstract description 2
- 238000001914 filtration Methods 0.000 abstract 1
- 230000003311 flocculating effect Effects 0.000 abstract 1
- 230000008092 positive effect Effects 0.000 abstract 1
- 230000001954 sterilising effect Effects 0.000 abstract 1
- 101150054854 POU1F1 gene Proteins 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000011001 backwashing Methods 0.000 description 3
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 241000269793 Cryothenia peninsulae Species 0.000 description 1
- 230000004308 accommodation Effects 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000000703 anti-shock Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005842 biochemical reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000010840 domestic wastewater Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 230000000116 mitigating effect Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Landscapes
- Physical Water Treatments (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model provides an integration laboratory wastewater treatment facility contains the collecting pit, and its technical essential lies in: the collecting pit passes through the elevator pump and connects the equalizing basin, and contact oxidation tank is connected to the equalizing basin, and this contact oxidation tank connects the flocculation basin that carries out flocculating reaction, and the flocculation basin passes through the membrane reactor and inserts the self priming pump, and the self priming pump meets activated carbon filter through the MBR symphysis, and this activated carbon filter connects gradually precision filter, booster pump, RO filtration membrane and ultraviolet sterilizing ware. The utility model has the advantages of with positive effect be: easy operation, the automated control of being convenient for, occupation space is little, high -efficient, energy -conserving intelligent laboratory wastewater processing apparatus.
Description
Technical field
This utility model is related to a kind of wastewater treatment equipment, particularly to lab sewage treatment equipment.
Background technology
At present, people have begun to factory's pollution, urban domestic wastewater are processed, and for the discharge of all kinds of laboratorys
Waste water pay attention to not, its pollution is usually ignored.Laboratory is actually the small-sized polluter of a quasi-representative, the waste water of discharge
Complicated component, containing substantial amounts of poisonous and harmful substances.A lot of laboratorys are located at city, are directly discharged into sewer and are formed and intersect dirt
Dye.With the strict demand improving constantly with environmental administration of people's environmental consciousness, row up to standard after the process of laboratory waste water needs
Put.
Because the discharge of wastewater situation of laboratory is complicated, the composition of the Pollutants in Wastewater of the laboratory of different operating property
Different.If directly processed using the pattern of industrialization wastewater treatment, it is extremely difficult to preferable treatment effect.At present, some
Laboratory Waste Water Treatment equipment, treatment effeciency is not high, and manual labor's intensity is big, and treatment effect is not ideal enough.
Compared with prior art, this utility model can remove most of metal ion and organic substance, effectively after mitigation
Biochemical treatment pressure.Biochemical treatment part, membrane bioreactor generation mud is few, processes load capacity by force, anti-shock loading
Ability is strong, and the pollution resistance of membrane reactor and reaction efficiency greatly improve, and the use of RO filter membrane has been completely secured water outlet
Water quality.
Content of the invention
This utility model is directed to the deficiencies in the prior art, provides lab sewage treatment equipment.
The purpose of this utility model is realized in：
Lab sewage treatment equipment, comprises collecting pit, and described collecting pit connects regulating reservoir by elevator pump, adjusts
Section pond connects contact-oxidation pool, and this contact-oxidation pool connects the flocculation basin carrying out flocculation reaction, and flocculation basin is connect by membrane reactor
Enter self priming pump, self priming pump connects active carbon filter by MBR film, this active carbon filter is sequentially connected accurate filter, increasing
Press pump, RO filter membrane and ultraviolet sterilizer.
Preferably, described collecting pit is provided with detachable filter, arranges collecting pit liquid level sensor inside collecting pit.
Preferably, described regulating reservoir setting regulating reservoir PH probe, regulating reservoir dosing tank and agitator.
Preferably, described contact-oxidation pool connects ozonator.
Preferably, described flocculation basin upper end arranges flocculation basin dosing tank, internal setting flocculation basin PH probe, and lower end setting is inhaled
Attached retention tank, described absorption retention tank connects membrane reactor.
Preferably, setting aerator and membrane reactor level sensor inside described membrane reactor.
Preferably, described RO filter membrane connects membrane reactor by reflux pump.
Preferably, described flocculation basin, contact-oxidation pool, ozonator and regulating reservoir upper end are provided with and connect overflowing of collecting pit
Head piece, described membrane reactor, flocculation basin, contact-oxidation pool, ozonator and regulating reservoir lower end are provided with the row connecting collecting pit
Liquid mouth.
Preferably, it is additionally provided with recoil loop between the qualified discharge pipe of described ultraviolet sterilizer and RO filter membrane.
The utility model has the advantage of：
This utility model is simple to operate, is easy to Automated condtrol, takes up room little, efficient, the intelligent laboratory of energy-conservation
Wastewater treatment equipment.
Brief description
Fig. 1 is structural representation of the present utility model；
In figure：1st, collecting pit；2nd, detachable filter；3rd, elevator pump；4th, regulating reservoir；5th, blender；6th, regulating reservoir PH visits
Head；7th, regulating reservoir dosing pump；8th, contact-oxidation pool；9th, ozonator；10th, flocculation basin；11st, flocculation basin dosing pump；12nd, adsorb
Retention tank；13rd, flocculation basin PH probe；14th, reflux pump；15th, membrane reactor；16th, aerator；17th, self priming pump；18th, MBR film；19、
Active carbon filter；20th, accurate filter；21st, booster pump；22nd, RO filter membrane；23rd, ultraviolet sterilizer；24th, backwashing pump.
Below in conjunction with accompanying drawing, by example, this utility model is further described, but following examples is only
Example in this utility model, does not represent the rights protection scope that this utility model is limited, power of the present utility model
Sharp protection domain is defined by claim.
Specific embodiment
Below in conjunction with the accompanying drawings specific embodiment of the present utility model is further illustrated：
As shown in figure 1, lab sewage treatment equipment, comprise collecting pit 1, described collecting pit 1 is provided with detachably
Filter 2, arranges collecting pit liquid level sensor inside collecting pit 1, and collecting pit 1 is connected with regulating reservoir PH by elevator pump 3
The regulating reservoir 4 of probe 6, regulating reservoir dosing tank 7 and agitator 5, this regulating reservoir 4 connects contact-oxidation pool 8, occurs installing ozone
The flocculation basin 10 carrying out flocculation reaction is connected, described flocculation basin 10 upper end arranges flocculation basin dosing tank after the contact-oxidation pool 8 of device 9
11, internal setting flocculation basin PH probe 13, lower end setting absorption retention tank 12, described absorption retention tank 12 connects membrane reactor
15, flocculation basin 10 accesses self priming pump 17 by membrane reactor 15, and described membrane reactor 15 is internal to arrange aerator 16 and film reaction
Device level sensor, self priming pump 17 connects active carbon filter 19 by MBR film 18, and this active carbon filter 19 is sequentially connected essence
Close filter 20, booster pump 21, RO filter membrane 22 and ultraviolet sterilizer 23, described RO filter membrane 22 passes through reflux pump 14 junctional membrane
Reactor 15, is additionally provided with recoil loop, recoils back between the qualified discharge pipe of described ultraviolet sterilizer 23 and RO filter membrane 22
It is provided with backwashing pump 24 in road.
In order to comprehensively be processed to waste water, described flocculation basin 10, contact-oxidation pool 8, ozonator 9 and regulating reservoir
4 upper ends are provided with the overfall connecting collecting pit 1, described membrane reactor 15, flocculation basin 10, contact-oxidation pool 8, ozonator 9
It is provided with, with regulating reservoir 4 lower end, the leakage fluid dram connecting collecting pit 1, wait that the waste water overflowing or discharging reenters whole wastewater treatment and sets
Standby.
Waste water enters collecting pit through detachable filter, controls elevator pump to enter by collecting pit liquid level sensor and adjusts
Pond, automatically adjusts pH value by regulating reservoir PH probe, after regulating reservoir dosing pump controls dosing, blender is stirred, by waste water
It is tuned into acidity, enter contact-oxidation pool, after being passed through ozone, flow to flocculation basin, add medicament, entering after carrying out abundant flocculation reaction
To 6-8, after separating, clear liquid enters membrane reactor to row acid-alkali accommodation pH value, and the mud of precipitation is transported at absorption retention tank, will carry
The clear liquid entering at absorption retention tank is again fed to membrane reactor.Flocculation pool inner water enters membrane bioreactor, starts aeration
Machine, after carrying out sufficient biochemical reaction, is extracted out by MBR film by self priming pump, through active carbon filter and accurate filter mistake
Pass through booster pump and RO filter membrane, the return of waste water of retention is to membrane reactor, pure water qualified discharge after ultraviolet-sterilization after filter.
Backwashing pump periodically recoils to RO filter membrane, is beneficial to the permeability keeping film.
In sum it is achieved that the purpose of this utility model.
These are only preferred embodiment of the present utility model, not in order to limit this utility model, all in this practicality
Within new spirit and principle, any modification, equivalent substitution and improvement made etc., should be included in guarantor of the present utility model
Within the scope of shield.
Claims (9)
1. lab sewage treatment equipment, comprises collecting pit, and it is technically characterized in that：Described collecting pit passes through elevator pump
Connect regulating reservoir, regulating reservoir connects contact-oxidation pool, this contact-oxidation pool connects the flocculation basin carrying out flocculation reaction, flocculation basin leads to
Cross membrane reactor and access self priming pump, self priming pump connects active carbon filter by MBR film, this active carbon filter is sequentially connected essence
Close filter, booster pump, RO filter membrane and ultraviolet sterilizer.
2. lab sewage treatment equipment according to claim 1 it is characterised in that：Described collecting pit is provided with can
Dismounting filter, arranges collecting pit liquid level sensor inside collecting pit.
3. lab sewage treatment equipment according to claim 1 it is characterised in that：Described regulating reservoir setting is adjusted
Section pond PH probe, regulating reservoir dosing tank and agitator.
4. lab sewage treatment equipment according to claim 1 it is characterised in that：Described contact-oxidation pool is even
Connect ozonator.
5. lab sewage treatment equipment according to claim 1 it is characterised in that：Described flocculation basin upper end sets
Put flocculation basin dosing tank, internal setting flocculation basin PH probe, lower end setting absorption retention tank, described absorption retention tank junctional membrane is anti-
Answer device.
6. lab sewage treatment equipment according to claim 1 it is characterised in that：Inside described membrane reactor
Setting aerator and membrane reactor level sensor.
7. lab sewage treatment equipment according to claim 1 it is characterised in that：Described RO filter membrane passes through
Reflux pump connects membrane reactor.
8. the lab sewage treatment equipment according to claim 4 it is characterised in that：Described flocculation basin, contact
Oxidation pond, ozonator and regulating reservoir upper end are provided with the overfall connecting collecting pit, described membrane reactor, flocculation basin, contact
Oxidation pond, ozonator and regulating reservoir lower end are provided with the leakage fluid dram connecting collecting pit.
9. lab sewage treatment equipment according to claim 1 it is characterised in that：Described ultraviolet sterilizer
It is additionally provided with recoil loop between qualified discharge pipe and RO filter membrane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620861105.0U CN205953776U (en) | 2016-08-10 | 2016-08-10 | Integration laboratory wastewater treatment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620861105.0U CN205953776U (en) | 2016-08-10 | 2016-08-10 | Integration laboratory wastewater treatment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205953776U true CN205953776U (en) | 2017-02-15 |
Family
ID=57975418
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620861105.0U Active CN205953776U (en) | 2016-08-10 | 2016-08-10 | Integration laboratory wastewater treatment facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205953776U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107089767A (en) * | 2017-05-19 | 2017-08-25 | 上海俊逸节能环保科技有限公司 | A kind of group technology of advanced treating laboratory sewage |
-
2016
- 2016-08-10 CN CN201620861105.0U patent/CN205953776U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107089767A (en) * | 2017-05-19 | 2017-08-25 | 上海俊逸节能环保科技有限公司 | A kind of group technology of advanced treating laboratory sewage |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190821 Address after: 110000 No. 165 Fengyang Road, Sujiatun District, Shenyang City, Liaoning Province Patentee after: Shenyang Maxinyu Technology Co., Ltd. Address before: 110 000 No. 360, Xia Changmao Village, Xia Changmao Tun, Huashan Street, Xingcheng City, Huludao City, Liaoning Province Patentee before: Zhao Wenlong |
|
| TR01 | Transfer of patent right |