CN107857442A - A kind of Laboratory Waste Water Treatment equipment - Google Patents
A kind of Laboratory Waste Water Treatment equipment Download PDFInfo
- Publication number
- CN107857442A CN107857442A CN201711322358.6A CN201711322358A CN107857442A CN 107857442 A CN107857442 A CN 107857442A CN 201711322358 A CN201711322358 A CN 201711322358A CN 107857442 A CN107857442 A CN 107857442A
- Authority
- CN
- China
- Prior art keywords
- air supporting
- treatment equipment
- waste water
- pond
- pool
- 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.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5281—Installations for water purification using chemical agents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/70—Treatment of water, waste water, or sewage by reduction
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/003—Wastewater from hospitals, laboratories and the like, heavily contaminated by pathogenic microorganisms
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/005—Processes using a programmable logic controller [PLC]
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/42—Liquid level
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Physical Water Treatments (AREA)
Abstract
The present invention solves the problems, such as traditional experiment room sewage treatment equipment automaticity difference.Laboratory Waste Water Treatment equipment, including controller, sewage collecting pool, air supporting stirring pool, redox pond, absorbent element, biological reaction apparatus and photochemical catalytic oxidation system.No.1 elevator pump and dosing tank group are provided between sewage collecting pool and air supporting stirring pool.Aerating pump is connected with air supporting stirring pool.No. two elevator pumps are provided between air supporting stirring pool and redox pond.Oxidation boost motor is connected with redox pond.No. three elevator pumps are provided between redox pond and absorbent element.No.1 elevator pump, No. two elevator pumps, No. three elevator pumps, aerating pump, dosing tank group and oxidation boost motor are connected with controller；The liquid level sensor being connected with controller is equipped with sewage collecting pool, in dosing tank group, in air supporting stirring pool and redox pond；The acidity-basicity sensor being connected with controller is provided with air supporting stirring pool.Automaticity of the present invention is high.
Description
Technical field
The present invention relates to Laboratory Waste Water Treatment field, more particularly to a kind of Laboratory Waste Water Treatment equipment.
Background technology
With the development of science and technology, it is more and more to the demand in laboratory, particularly in recent ten years, all kinds of laboratories
Quantity is continuously increased.From the point of view of the distribution in laboratory, be concentrated mainly on the universities and colleges such as middle and high, scientific research institutions, medical institutions,
The industries such as bio-pharmaceuticals, disease control, ring prison, product quality, drug inspection, blood station, herding, hospital, enterprise, laboratory waste water discharge
Amount is little, and its pollution is easy to ignored.
Laboratory is actually the serious pollution sources of a quasi-representative, and pollutant is usually ignored by people, more, the dirt of construction
The total amount of dye is bigger.Waste water caused by laboratory typically without underground sewage pipe network is directly discharged into after processing or simple process, is sent
Focused on to large-scale sewage treatment plants.Due to laboratory sewage composition complexity, the lead particularly contained, mercury, cadmium, sexavalence
The disease-producing pathogens such as the heavy metals such as chromium, copper, antimony, ferrous iron, aluminium, manganese and substantial amounts of bacterium, virus, worm's ovum, also chemical drugs
Agent and radio isotope etc., the facility of sewage treatment plants can only finally be discharged into rivers to its " helpless ".These realities
Room is tested, it is especially especially big in harm of the chemical laboratory of inner city and residential block to environment, because many chemical experiments
The drainage pipeline of room communicates with the drainage pipeline of resident, and pollutant forms cross pollution, acute infection by sewer and hidden
Property the feature that infects finally flow into rivers or permeate the ground, after heavy metal enters water source or soil, a variety of ways may be passed through
Footpath enters the food chain of the mankind.
Traditional experiment room sewage treatment equipment has the following disadvantages：
1st, traditional experiment room sewage treatment equipment, typically using buried or ground integral type, floor space is big, typically
Suitable for the big discharge capacity of industrial enterprise, for laboratory small emission, product, which takes up an area, to be needed to minimize.
2nd, after traditional experiment room sewage treatment equipment realizes nothing but the automation and the processing of each link of each link
The detection of data result.
3rd, using acid-base neutralization regulation, coagulation dosing reaction, filtering on traditional experiment room sewage treatment equipment general technology
The techniques such as precipitation, can not be comprehensive due to various organic pollutions, inorganic pollution and biological pollutant in laboratory waste water
Handle every pollutant.
4th, using acid-base neutralization regulation, coagulation dosing reaction, filtering on traditional experiment room sewage treatment equipment general technology
The techniques such as precipitation, can not be comprehensive due to various organic pollutions, inorganic pollution and biological pollutant in laboratory waste water
Handle every pollutant.
5th, traditional experiment room sewage treatment equipment typically uses simple industry control mode, complex operation, program trouble.
6th, traditional experiment room sewage treatment equipment exhausts prompt facility without medicament.Also stopping function is exhausted without medicament.Such as medicine
Case medicament exhausts equipment and continued to run with waste water is not effectively addressed, and influences drainage index.
The content of the invention
The invention provides a kind of Laboratory Waste Water Treatment equipment, it is intended to it is automatic to solve traditional experiment room sewage treatment equipment
The problem of change degree is poor.
In order to solve the above technical problems, the present invention is achieved through the following technical solutions：
A kind of Laboratory Waste Water Treatment equipment, sewage disposal system and the controller with display screen, sewage disposal system
According to sewage disposal order, being from upstream to downstream includes passing sequentially through the connected sewage collecting pool of pipeline, air supporting stirring pool, oxidation
Reduce pond, absorbent element, biological reaction apparatus and photochemical catalytic oxidation system.Between the sewage collecting pool and air supporting stirring pool
Pipeline be provided with No.1 elevator pump and dosing tank group, dosing tank group includes alkali case, sour case and PAC casees.The air supporting stirring pool
On be connected with aerating pump.Pipeline between the air supporting stirring pool and redox pond is provided with No. two elevator pumps.The oxidation
Reduction is connected with oxidation boost motor on pond.Pipeline between the redox pond and absorbent element is provided with No. three liftings
Pump.The absorbent element be from upstream to downstream include be sequentially connected secondary absorption system, light electrolysis absorber, heavy metal inhale
Adnexa and organic matter absorber.The No.1 elevator pump, No. two elevator pumps, No. three elevator pumps, aerating pump and dosing tank group with
Controller is connected；It is equipped with and controller phase in sewage collecting pool, in dosing tank group, in air supporting stirring pool and redox pond
Liquid level sensor even；The acidity-basicity sensor being connected with controller is provided with air supporting stirring pool.
Further, sewage disposal system also includes sludge drying device, and sludge drying device is provided with discharge outlet and mud inlet, sludge
The discharge outlet of drying device is connected by pipeline with sewage collecting pool, and the mud inlet of sludge drying device passes through pipeline and air supporting stirring pool
It is connected and is connected with redox pond；Pipeline between the mud inlet and air supporting stirring pool of the mud drying device is provided with No.1 spoil disposal
Valve, No. two mud valves are connected with the pipeline between the mud inlet of the mud drying device and redox pond.
Further, sewage disposal system also includes purging system, purging system include No.1 cleaning pipe, No. two cleaning pipes and
No. three cleaning pipes；The No.1 cleaning pipe is connected between water source and secondary absorption system, and is connected with punching on No.1 cleaning pipe
Wash valve；No. two cleanings pipe is connected between water source and biological reaction apparatus, and is connected with backwash water intaking valve on No. two cleaning pipes；
No. three cleanings pipe is connected between water source and biological reaction apparatus, and is connected with No. three cleaning pipes and is just washed water intaking valve.
Further, the both ends of biological reaction apparatus, which are respectively equipped with, just washes drainpipe and backwash drainpipe；Just wash on drainpipe
Provided with positive valve, backwash drainpipe is provided with anti-valve.
Further, production water valve is provided between the biological reaction apparatus and photochemical catalytic oxidation system.Light is flowed to for controlling
The size of catalytic oxidation system current.
Further, the secondary absorption of secondary absorption system is respectively charcoal absorption and quartz sand absorption.
Further, it is equipped with redox pond and in photochemical catalytic oxidation system the conductance probe head being connected with controller.
Further, the controller is PLC or single-chip microcomputer.
Compared with prior art it is an advantage of the invention that：
Dosing tank group is connected with controller in the present invention, is provided with air supporting stirring pool in air supporting stirring pool and is provided with and controller
Connected acidity-basicity sensor, the waste water of various concentrations index can be directed to, oneself adjusts its dosing reaction time；Whole process
Full automatic treatment waste water, for the composition and concentration of different waste water, controller is carried out calculating and then carried out in proportion automatic automatically
Launch medicine.
The liquid level sensor being connected with controller is provided with the present invention in dosing tank group, possesses medicine-chest medicament and exhausts prompting work(
Can, and can be out of service after medicament exhausts, continued to run with addition medicament rear.Ensure discharge it is each drip all be by
It is qualified treated.
Controller is provided with display screen in the present invention, it is possible to achieve man-machine interaction, data display management, display each unit operation
State, such as cartoon type flow chart or with form, block diagram or trend diagram form show each processing unit real-time running data,
Historical data, alert data, running status, running rate statistics and discharge capacity.
About 8-12 squares of floor space of the present invention, floor space is small, and processing speed is fast, installs conveniently moving, is truly realized
Engineering equipment, good appearance, it is not necessary to dig multiple processing ponds.
Brief description of the drawings
In order to illustrate the technical solution of the embodiments of the present invention more clearly, below by embodiment it is required use it is attached
Figure is briefly described, it will be appreciated that the following drawings illustrate only certain embodiments of the present invention, therefore be not to be taken as to model
The restriction enclosed, for those of ordinary skill in the art, on the premise of not paying creative work, can also be according to these
Accompanying drawing obtains other related accompanying drawings.
Fig. 1 is the system principle schematic diagram of the present invention.
Embodiment
In the description of the invention, unless otherwise clearly defined and limited, term " installation ", " connected ", " connection ",
Terms such as " fixations " should be interpreted broadly, for example, it may be fixedly connected or be detachably connected, or integrally；Can be with
It is mechanical connection or electrical connection；Can be directly connected to or be indirectly connected by intermediary, Ke Yishi
The connection of two element internals or the interaction relationship of two elements.For those of ordinary skills, Ke Yigen
Understand the concrete meaning of above-mentioned term in the present invention according to concrete condition.
Refering to Fig. 1, a kind of Laboratory Waste Water Treatment equipment, sewage disposal system and the controller with display screen, sewage
Processing system is from upstream to downstream and stirred including passing sequentially through sewage collecting pool 1, air supporting that pipeline is connected according to sewage disposal order
Pond 5, redox pond 6, absorbent element, biological reaction apparatus 21 and photochemical catalytic oxidation system 26 are mixed, sewage passes through last
After the processing for walking photochemical catalytic oxidation system 26, drainage system 27 is flowed to.
Pipeline between the sewage collecting pool 1 and air supporting stirring pool 5 is provided with No.1 elevator pump 34 and dosing tank group, adds
Medicine-chest group includes alkali case 2, sour case 3 and PAC casees 4.
Aerating pump 35 is connected with the air supporting stirring pool 5.
Pipeline between the air supporting stirring pool 5 and redox pond 6 is provided with No. two elevator pumps 30.
The oxidation boost motor 36 being connected with controller is connected with the redox pond 6, oxidation boost motor 36 is oxidation
Reduce the medicament that redox reaction is provided in pond.
Pipeline between the redox pond 6 and absorbent element is provided with No. three elevator pumps 28.
The absorbent element be from upstream to downstream include be sequentially connected secondary absorption system 9, light electrolysis absorber 10,
Heavy metal adsorption device 11 and organic matter absorber 12.
The elevator pump 30, three of No.1 elevator pump 34, two elevator pump 28, aerating pump 35 and the dosing tank group with control
Device is connected；It is equipped with and controller phase in sewage collecting pool 1, in dosing tank group, in air supporting stirring pool 5 and redox pond 6
Liquid level sensor even；The acidity-basicity sensor being connected with controller is provided with air supporting stirring pool 5.
Sewage disposal system also includes sludge drying device 33, and sludge drying device is provided with discharge outlet and mud inlet, sludge drying
The discharge outlet of device 33 is connected by pipeline with sewage collecting pool 1, and the mud inlet of sludge drying device passes through pipeline and air supporting stirring pool 5
It is connected and is connected with redox pond；Pipeline between the mud inlet and air supporting stirring pool 5 of the mud drying device 33 is provided with No.1
Mud valve 31, No. two mud valves 29, mud are connected with the pipeline between the mud inlet of the mud drying device 33 and redox pond 6
The mud inlet of drying device 33 is provided with slush pump 32.
Sewage disposal system also includes purging system, and purging system includes 8, No. two cleaning pipes 20 of No.1 cleaning pipe and No. three
Clean pipe 14；The No.1 cleaning pipe 8 is connected between water source 13 and secondary absorption system 9, and is connected with No.1 cleaning pipe 8
Flushing valve 7；No. two cleanings pipe 20 is connected between water source 13 and biological reaction apparatus 21, and is connected with No. two cleaning pipes 20
Backwash water intaking valve 19；No. three cleanings pipe 14 is connected between water source 13 and biological reaction apparatus 21, and No. three cleaning pipes 14
On be connected with and just wash water intaking valve 15.The both ends of biological reaction apparatus 21, which are respectively equipped with, just washes drainpipe 23 and backwash drainpipe 16；Just
Wash drainpipe 23 and be provided with positive valve 24, backwash drainpipe 16 is provided with anti-valve 17；Just washing the current direction of the discharge of drainpipe 23
Just washing collecting tank 25, the current direction backwash collecting tank 18 that backwash drainpipe 16 is discharged；Just washing collecting tank 25 and backwash collecting tank 18
Interior Water Sproading is in sewage collecting pool 1.
Pipeline between biological reaction apparatus 21 and photochemical catalytic oxidation system 26 is provided with production water valve 22.
The secondary absorption of secondary absorption system 9 is respectively charcoal absorption and quartz sand absorption.
The conductance probe head being connected with controller is equipped with redox pond 6 and in photochemical catalytic oxidation system 26.
The controller is PLC or single-chip microcomputer.
With reference to operation principle, the present invention will be further described：
Sewage enters sewage collecting pool 1, then in turn through air supporting stirring pool 5, redox pond 6, absorbent element, life
Thing reaction unit 21 and photochemical catalytic oxidation system 26, after processing of the sewage by final step photochemical catalytic oxidation system 26, flow direction
Drainage system 27.
When sewage is located at low liquid level into sewage collecting pool 1 or when air supporting stirring pool 5 is located at high level, No.1 elevator pump
34 are stopped.When air supporting stirring pool 5 is located at low liquid level or when redox pond 6 is located at high level, No. two elevator pumps 30, stop
Only work.When being located at low liquid level in redox pond 6, No. three elevator pumps 28 are stopped.Sewage collecting pool 1 is interior, air supporting stirring
Liquid level in pond 5 and in redox pond 6 is detected by liquid level sensor.
Sludge drying device 33 extracts the sludge that air supporting stirring pool 5 is connected and redox pond 6 is precipitated by slush pump 32, right
Sludge is handled, and the moisture in sludge can be recycled in sewage collecting pool 1.
After sewage flows into air supporting stirring pool 5, first pass through alkali case 2 and add the alkalescence that alkali is adjusted to setting, then pass through PAC casees 4
Add PAC and carry out flocculation sediment, acid is then added by sour case 3 and neutralized.Added by acidity-basicity sensor and controller pair
Medicine-chest group is strictly automatically controlled.
In redox pond 6, medicament is added by aoxidizing boost motor 36, sewage carries out redox reaction, Aid for Oxidation
Thruster 36 adds medicament and is controlled by controller.
After sewage is handled through oxidization-reduction pond 6, successively by secondary absorption system 9, light electrolysis absorber 10, heavy metal
The adsorption treatment of absorber 11 and organic matter absorber 12, subsequently into biological reaction apparatus 21.
Secondary absorption system 9 and biological reaction apparatus 21 are cleaned using purging system timing.In purging system
Water source 13 is municipal water sources.When opening flushing valve 7, the water in water source 13 cleans pipe 8 by No.1 and flows into secondary absorption system 9,
Secondary absorption system 9 is cleaned.When opening backwash water intaking valve 19 and anti-valve 17, the water at water source 13 is managed by No. two cleanings
20 enter biological reaction apparatus 21, biological reaction apparatus 21 are backwashed, the water after backwash flows into instead from backwash drainpipe 16
Wash collecting tank 18.When opening is just washing water intaking valve 15 and positive valve 24, the water in water source 13 flows into biology by No. three cleaning pipes 14
Reaction unit 21, biological reaction apparatus 21 is just being rinsed, the water after positive flushing flows out from drainpipe 23 is just washed, and enters and just wash receipts
Collect groove 25.
The present invention can in the waste water of collection, processing procedure, handled after the qualified discharge water of discharge carry out PH, conductance
Rate, turbidity are monitored on-line.Separately there is exceeded setting management：Setting allows to discharge supplemental characteristic alarm limits, such as discharges parameter
Numerical value exceedes setting limit value, remote monitoring system and host service function main interface meeting automatic alarm and shows exceeded parameter, controller
Start limiting emission program, while start overstandard waste water and carry out reflow treatment program, and keep track of, after processing is up to standard
Can automatic-discharging.
The present invention can be directed to the waste water of various concentrations index, oneself adjust its dosing reaction time, and whole process is complete certainly
Dynamic processing waste water, composition and concentration for different waste water, controller are carried out calculating and then launched automatically in proportion automatically
Medicine.
Controller of the present invention completes electric and meter section automatic control using Siemens's programmable logic controller (PLC) (PLC)
System and monitoring, equipment electric-control system when 10 inches of Delta LCD liquid crystal touch screens Chinese displays can realize interactive mode, start
Automatic detection.Interactive mode, data display management can be realized：Liquid crystal display each unit running status is digitized, it is such as dynamic
Picture formula flow chart shows each processing unit liquid level, flow, hydraulic pressure, temperature, electricity with form, block diagram or trend diagram form
The real-time running data of the parts such as pressure, electric current, anti-corrosion elevator pump, instrument and meter, monitoring device, historical data, alert data, fortune
Row state, running rate statistics, discharge capacity.
The present invention possesses medicine-chest medicament and exhausts prompt facility, and can be out of service after medicament exhausts, after medicament is added,
It can just continue to run with.Each drip for ensureing to be discharged into city planting ductwork is all by qualified processing.
The specific embodiment of the present invention is the foregoing is only, but the technical characteristic of the present invention is not limited thereto, Ren Heben
The technical staff in field in the field of the invention, all cover among the scope of the claims of the present invention by the change or modification made.
Claims (8)
1. a kind of Laboratory Waste Water Treatment equipment, it is characterized in that：Sewage disposal system and the controller with display screen, at sewage
According to sewage disposal order, be from upstream to downstream includes passing sequentially through the connected sewage collecting pool of pipeline, air supporting stirring reason system
Pond, redox pond, absorbent element, biological reaction apparatus and photochemical catalytic oxidation system；
Pipeline between the sewage collecting pool and air supporting stirring pool is provided with No.1 elevator pump and dosing tank group, dosing tank group bag
Include alkali case, sour case and PAC casees；
Aerating pump is connected with the air supporting stirring pool；
Pipeline between the air supporting stirring pool and redox pond is provided with No. two elevator pumps；
Oxidation boost motor is connected with the redox pond；
Pipeline between the redox pond and absorbent element is provided with No. three elevator pumps；
The absorbent element be from upstream to downstream include be sequentially connected secondary absorption system, light electrolysis absorber, heavy metal
Absorber and organic matter absorber；
The No.1 elevator pump, No. two elevator pumps, No. three elevator pumps, aerating pump, dosing tank group and oxidation boost motor with control
Device is connected；It is equipped with what is be connected with controller in sewage collecting pool, in dosing tank group, in air supporting stirring pool and redox pond
Liquid level sensor；The acidity-basicity sensor being connected with controller is provided with air supporting stirring pool.
2. a kind of Laboratory Waste Water Treatment equipment according to claim 1, it is characterized in that：Sewage disposal system also includes dirt
Mud drying device, sludge drying device are provided with discharge outlet and mud inlet, and the discharge outlet of sludge drying device passes through pipeline and sewage collecting pool
It is connected, the mud inlet of sludge drying device is connected by pipeline with air supporting stirring pool and redox pond is connected；The mud drying device
Mud inlet and air supporting stirring pool between pipeline be provided with No.1 mud valve, the mud inlet of the mud drying device and redox
No. two mud valves are connected with pipeline between pond.
3. a kind of Laboratory Waste Water Treatment equipment according to claim 1, it is characterized in that：Sewage disposal system also includes clear
System is washed, purging system includes No.1 cleaning pipe, No. two cleaning pipes and No. three cleaning pipes；The No.1 cleaning pipe is connected to water source
Between secondary absorption system, and flushing valve is connected with No.1 cleaning pipe；No. two cleanings pipe is connected to water source and biology
Between reaction unit, and backwash water intaking valve is connected with No. two cleaning pipes；No. three cleanings pipe is connected to water source and biological respinse
Between device, and it is connected with No. three cleaning pipes and just washes water intaking valve.
4. a kind of Laboratory Waste Water Treatment equipment according to claim 3, it is characterized in that：The both ends of biological reaction apparatus point
It She You not just wash drainpipe and backwash drainpipe；Just washing drainpipe and be provided with positive valve, backwash drainpipe is provided with anti-valve.
5. a kind of Laboratory Waste Water Treatment equipment according to claim 1, it is characterized in that：The biological reaction apparatus and light
Production water valve is provided between catalytic oxidation system.
6. a kind of Laboratory Waste Water Treatment equipment according to claim 1, it is characterized in that：The two level of secondary absorption system is inhaled
Attached is respectively charcoal absorption and quartz sand absorption.
7. a kind of Laboratory Waste Water Treatment equipment according to claim 1, it is characterized in that：In redox pond and photocatalysis
The conductance probe head being connected with controller is equipped with oxidative system.
8. a kind of Laboratory Waste Water Treatment equipment according to any one of claims 1 to 7, it is characterized in that：The controller is
PLC or single-chip microcomputer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711322358.6A CN107857442A (en) | 2017-12-12 | 2017-12-12 | A kind of Laboratory Waste Water Treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711322358.6A CN107857442A (en) | 2017-12-12 | 2017-12-12 | A kind of Laboratory Waste Water Treatment equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107857442A true CN107857442A (en) | 2018-03-30 |
Family
ID=61706225
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711322358.6A Pending CN107857442A (en) | 2017-12-12 | 2017-12-12 | A kind of Laboratory Waste Water Treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107857442A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109302670A (en) * | 2018-10-18 | 2019-02-01 | 珠海格力电器股份有限公司 | Facility information display methods, server, device and system |
| CN109940787A (en) * | 2019-03-01 | 2019-06-28 | 南京信息工程大学 | A kind of processing system and its processing method of chemical reagent plastics empty bottle |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101024534A (en) * | 2006-02-21 | 2007-08-29 | 中国科学院生态环境研究中心 | Biological electrochemical combined system for treating dye waste water and method thereof |
| CN101041536A (en) * | 2007-04-30 | 2007-09-26 | 李保标 | Integrated waste water treating machine |
| CN102807298A (en) * | 2011-05-31 | 2012-12-05 | 北京湘顺源科技有限公司 | Laboratory comprehensive waste water centralization treatment apparatus |
| CN202785890U (en) * | 2012-09-26 | 2013-03-13 | 武汉方元环境科技股份有限公司 | Advanced treatment and recycling device for textile printing and dyeing wastewater |
| CN203845900U (en) * | 2014-05-09 | 2014-09-24 | 南京晓庄学院 | Organic sewage treatment device in lab |
| CN104909490A (en) * | 2015-05-19 | 2015-09-16 | 东风活塞轴瓦有限公司 | Phosphating and chemical nickel-plating mixed comprehensive wastewater treatment process and automated device |
| CN206607129U (en) * | 2017-03-22 | 2017-11-03 | 云南省环境科学研究院(中国昆明高原湖泊国际研究中心) | A kind of apparatus for treating carbonized waste water |
| CN207699417U (en) * | 2017-12-12 | 2018-08-07 | 四川卓越水处理设备有限公司 | A kind of Laboratory Waste Water Treatment equipment |
-
2017
- 2017-12-12 CN CN201711322358.6A patent/CN107857442A/en active Pending
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101024534A (en) * | 2006-02-21 | 2007-08-29 | 中国科学院生态环境研究中心 | Biological electrochemical combined system for treating dye waste water and method thereof |
| CN101041536A (en) * | 2007-04-30 | 2007-09-26 | 李保标 | Integrated waste water treating machine |
| CN102807298A (en) * | 2011-05-31 | 2012-12-05 | 北京湘顺源科技有限公司 | Laboratory comprehensive waste water centralization treatment apparatus |
| CN202785890U (en) * | 2012-09-26 | 2013-03-13 | 武汉方元环境科技股份有限公司 | Advanced treatment and recycling device for textile printing and dyeing wastewater |
| CN203845900U (en) * | 2014-05-09 | 2014-09-24 | 南京晓庄学院 | Organic sewage treatment device in lab |
| CN104909490A (en) * | 2015-05-19 | 2015-09-16 | 东风活塞轴瓦有限公司 | Phosphating and chemical nickel-plating mixed comprehensive wastewater treatment process and automated device |
| CN206607129U (en) * | 2017-03-22 | 2017-11-03 | 云南省环境科学研究院(中国昆明高原湖泊国际研究中心) | A kind of apparatus for treating carbonized waste water |
| CN207699417U (en) * | 2017-12-12 | 2018-08-07 | 四川卓越水处理设备有限公司 | A kind of Laboratory Waste Water Treatment equipment |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109302670A (en) * | 2018-10-18 | 2019-02-01 | 珠海格力电器股份有限公司 | Facility information display methods, server, device and system |
| CN109302670B (en) * | 2018-10-18 | 2020-10-09 | 珠海格力电器股份有限公司 | Equipment information display method, server, device and system |
| CN109940787A (en) * | 2019-03-01 | 2019-06-28 | 南京信息工程大学 | A kind of processing system and its processing method of chemical reagent plastics empty bottle |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN109607982A (en) | A kind of laboratory integration waste water treatment system | |
| CN106673168A (en) | Laboratory waste liquid collection and treatment device | |
| CN111439877A (en) | Intelligent urban rainwater treatment device and analysis system | |
| CN215208825U (en) | Waste water treatment device for stone processing | |
| CN207699417U (en) | A kind of Laboratory Waste Water Treatment equipment | |
| CN207525086U (en) | A kind of rotary-type sewage-treatment plant | |
| CN110482748A (en) | A kind of laboratory waste liquid processing unit | |
| CN107857442A (en) | A kind of Laboratory Waste Water Treatment equipment | |
| CN109336222A (en) | Immersion gravity stream ceramic membrane microkinetic ultrafiltration system sewage disposal device and method | |
| KR100367219B1 (en) | An equipment of advanced drinking water treatment for the control of micro-pollutants | |
| CN110526509A (en) | A kind of intelligent and high-efficiency sewage disposal system | |
| CN205528144U (en) | Medical treatment type waste water treatment equipment | |
| CN209383616U (en) | Buried Internet of Things intelligent sewage treatment plant | |
| CN208869445U (en) | Integrated sewage treating apparatus | |
| CN207699409U (en) | A kind of modularization sewage-treatment plant | |
| CN214936726U (en) | Waste water purification and recovery device | |
| CN108751520A (en) | A kind of circulating high-efficiency sewage treatment and purification equipment | |
| CN108689527A (en) | A kind of sewage disposal sterilised filtration pond | |
| CN205442990U (en) | Sewage purification processing device | |
| CN108083540A (en) | A kind of desk type water purification | |
| CN105858980A (en) | CODcr wastewater treatment system and treatment method thereof | |
| CN209210442U (en) | A kind of immersion gravity stream ceramic membrane microkinetic ultrafiltration system sewage disposal device | |
| CN209923150U (en) | Oligodynamic domestic sewage treatment device | |
| CN208308647U (en) | Wastewater degradation device is used in a kind of production of dichloro-nicotinic acid | |
| CN205803182U (en) | CODcr liquid waste treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |