CN207699417U - A kind of Laboratory Waste Water Treatment equipment - Google Patents
A kind of Laboratory Waste Water Treatment equipment Download PDFInfo
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- CN207699417U CN207699417U CN201721729178.5U CN201721729178U CN207699417U CN 207699417 U CN207699417 U CN 207699417U CN 201721729178 U CN201721729178 U CN 201721729178U CN 207699417 U CN207699417 U CN 207699417U
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- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 16
- 239000010865 sewage Substances 0.000 claims abstract description 55
- 238000003756 stirring Methods 0.000 claims abstract description 36
- 238000006243 chemical reaction Methods 0.000 claims abstract description 24
- 230000003647 oxidation Effects 0.000 claims abstract description 23
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 23
- 230000003197 catalytic effect Effects 0.000 claims abstract description 13
- 239000007788 liquid Substances 0.000 claims abstract description 13
- 239000002250 absorbent Substances 0.000 claims abstract description 12
- 230000002745 absorbent Effects 0.000 claims abstract description 12
- 238000004140 cleaning Methods 0.000 claims description 37
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 25
- 239000010802 sludge Substances 0.000 claims description 22
- 238000001035 drying Methods 0.000 claims description 20
- 238000010521 absorption reaction Methods 0.000 claims description 18
- 239000006096 absorbing agent Substances 0.000 claims description 10
- 238000005406 washing Methods 0.000 claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- 238000011144 upstream manufacturing Methods 0.000 claims description 6
- 239000003513 alkali Substances 0.000 claims description 5
- 229910001385 heavy metal Inorganic materials 0.000 claims description 5
- 238000001179 sorption measurement Methods 0.000 claims description 5
- 238000005868 electrolysis reaction Methods 0.000 claims description 4
- 238000011010 flushing procedure Methods 0.000 claims description 4
- 239000005416 organic matter Substances 0.000 claims description 4
- 239000006004 Quartz sand Substances 0.000 claims description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 239000000523 sample Substances 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims 1
- 230000001590 oxidative effect Effects 0.000 claims 1
- 229910052760 oxygen Inorganic materials 0.000 claims 1
- 239000001301 oxygen Substances 0.000 claims 1
- 230000001699 photocatalysis Effects 0.000 claims 1
- 238000007146 photocatalysis Methods 0.000 claims 1
- 238000002474 experimental method Methods 0.000 abstract description 10
- 239000003814 drug Substances 0.000 description 17
- 239000002351 wastewater Substances 0.000 description 13
- 238000012545 processing Methods 0.000 description 11
- 239000003344 environmental pollutant Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 231100000719 pollutant Toxicity 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 229940079593 drug Drugs 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 3
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- 239000002585 base Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 201000010099 disease Diseases 0.000 description 2
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 230000003993 interaction Effects 0.000 description 2
- 230000002452 interceptive effect Effects 0.000 description 2
- 239000004973 liquid crystal related substance Substances 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 230000035484 reaction time Effects 0.000 description 2
- 238000006479 redox reaction Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 241001269238 Data Species 0.000 description 1
- 102000002322 Egg Proteins Human genes 0.000 description 1
- 108010000912 Egg Proteins Proteins 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000001154 acute effect Effects 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052787 antimony Inorganic materials 0.000 description 1
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 1
- 229960000074 biopharmaceutical Drugs 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
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- 238000012864 cross contamination Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
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- 238000007599 discharging Methods 0.000 description 1
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- 239000000284 extract Substances 0.000 description 1
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- 208000015181 infectious disease Diseases 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011572 manganese Substances 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012806 monitoring device Methods 0.000 description 1
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- 230000002285 radioactive effect Effects 0.000 description 1
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- 239000013049 sediment Substances 0.000 description 1
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- 239000002689 soil Substances 0.000 description 1
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- Physical Water Treatments (AREA)
Abstract
The utility model solves the problems, such as that traditional experiment room sewage treatment equipment the degree of automation is poor.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 equipped between sewage collecting pool and air supporting stirring pool.Aerating pump is connected on air supporting stirring pool.No. two elevator pumps are equipped between air supporting stirring pool and redox pond.Oxidation boost motor is connected on redox pond.No. three elevator pumps are equipped 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；It is equipped with the liquid level sensor being connected with controller in sewage collecting pool, in dosing tank group, in air supporting stirring pool and redox pond；The acidity-basicity sensor being connected with controller is equipped in air supporting stirring pool.The utility model high degree of automation.
Description
Technical field
The utility model is related 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, more and more to the demand in laboratory, especially 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 middle and high equal universities and colleges, 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 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.The waste water that laboratory generates is sent generally without underground sewage pipe network is directly discharged into after processing or simple process
It is focused on to large-scale sewage treatment plants.Due to laboratory sewage composition complexity, the lead especially contained, mercury, cadmium, sexavalence
The disease-producing pathogens such as the heavy metals such as chromium, copper, antimony, ferrous iron, aluminium, manganese and a large amount of bacterium, virus, worm's ovum, also chemical drugs
The facility of agent and radioactive isotope etc., sewage treatment plants can only finally be discharged into rivers to its " helpless ".These realities
Room is tested, it is especially especially big to the harm of environment in the chemical laboratory of inner city and residential block, because of many chemical experiments
The drainage pipeline of room is communicated with the drainage pipeline of resident, and pollutant forms cross contamination, acute infection by sewer and hides
Property infect feature finally flow into rivers or permeate the ground, after heavy metal enters water source or soil, a variety of ways may be passed through
Diameter enters the food chain of the mankind.
Traditional experiment room sewage treatment equipment has the following disadvantages：
1, traditional experiment room sewage treatment equipment generally uses buried or ground integral type, takes up a large area, generally
Suitable for the big discharge capacity of industrial enterprise, for laboratory small emission, product occupation of land needs to minimize.
2, after traditional experiment room sewage treatment equipment realizes that nothing but the automation of each link and each link are handled
The detection of data result.
3, it adjusted, coagulation dosing reaction, filtered using acid-base neutralization 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
The every pollutant of processing.
4, it adjusted, coagulation dosing reaction, filtered using acid-base neutralization 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
The every pollutant of processing.
5, traditional experiment room sewage treatment equipment generally uses simple industry control mode, complicated for operation, program trouble.
6, 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 continues to run with waste water is not effectively addressed, and influences drainage index.
Utility model content
The utility model provides a kind of Laboratory Waste Water Treatment equipment, it is intended to solve traditional experiment room sewage treatment equipment
The poor problem of the degree of automation.
In order to solve the above technical problems, the utility model 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 sequence, it includes passing sequentially through the connected sewage collecting pool of pipeline, air supporting stirring pool, oxidation to be from upstream to downstream
Restore pond, absorbent element, biological reaction apparatus and photochemical catalytic oxidation system.Between the sewage collecting pool and air supporting stirring pool
Pipeline be equipped 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 equipped 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 equipped with No. three promotions
Pump.It includes the secondary absorption system being sequentially connected, light electrolysis absorber, heavy metal suction that the absorbent element, which is from upstream to downstream,
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 equipped in air supporting stirring pool.
Further, sewage disposal system further includes sludge drying device, and sludge drying device is equipped 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 sludge drying device is arranged equipped with No.1
Slurry valve is connected with No. two mud valves on the pipeline between the mud inlet and redox pond of the sludge drying device.
Further, sewage disposal system further includes cleaning system, cleaning 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 punching is connected in No.1 cleaning pipe
Wash valve；No. two cleaning pipes are connected between water source and biological reaction apparatus, and are connected with backwash inlet valve in No. two cleaning pipes；
No. three cleaning pipes are connected between water source and biological reaction apparatus, and are connected in No. three cleaning pipes and are just washed inlet valve.
Further, the both ends of biological reaction apparatus, which are respectively equipped with, just washes drainpipe and backwash drainpipe；Just wash on drainpipe
Equipped with positive valve, backwash drainpipe is equipped with anti-valve.
Further, production water valve is equipped between the biological reaction apparatus and photochemical catalytic oxidation system.Light is flowed to for controlling
The size of catalytic oxidation system flow.
Further, the secondary absorption of secondary absorption system is respectively activated carbon adsorption and quartz sand absorption.
Further, it is equipped with the conductance probe head being connected with controller in redox pond and in photochemical catalytic oxidation system.
Further, the controller is PLC or microcontroller.
Compared with prior art the utility model has the advantages that：
Dosing tank group is connected with controller in the utility model, is equipped in air supporting stirring pool and is equipped with and control in air supporting stirring pool
The connected acidity-basicity sensor of device processed can be directed to the waste water of various concentration index, oneself adjust its dosing reaction time；Entirely
Process full automatic treatment waste water, for the ingredient and concentration of different waste water, then controller carries out calculating automatically to carry out in proportion
It is automatic to launch drug.
The liquid level sensor being connected with controller is equipped in the utility model in dosing tank group, has medicine-chest medicament and exhausts and carry
Show function, and can be out of service after medicament exhausts, is continued to run at addition medicament rear.Ensureing each drip of discharge is all
By qualified processed.
Controller is equipped with display screen in the utility model, and human-computer interaction may be implemented, and data display management shows each unit
Operating status shows the real time execution of each processing unit such as cartoon type flow chart or with table, block diagram or trend diagram form
Data, historical data, alert data, operating status, running rate statistics and discharge capacity.
About 8-12 squares of the utility model floor space, floor space is small, and processing speed is fast, installs conveniently moving, really
Accomplish that engineering equipment, good appearance need not dig multiple processing ponds.
Description of the drawings
It, below will be to required use in embodiment in order to illustrate more clearly of the technical solution of the utility model embodiment
Attached drawing be briefly described, it should be understood that the following drawings illustrates only some embodiments of the utility model, therefore should not see
Work is the restriction to range, for those of ordinary skill in the art, without creative efforts, can be with
Other relevant attached drawings are obtained according to these attached drawings.
Fig. 1 is the system principle schematic diagram of the utility model.
Specific implementation mode
In the description of the present invention, unless otherwise clearly defined and limited, term " installation ", " connected ", " company
Connect ", the terms such as " fixation " 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, can also be electrical connection；Can be directly connected to, can also be indirectly connected through an intermediary, can
To be the interaction relationship of connection or two elements inside two elements.For those of ordinary skills, may be used
To understand the concrete meaning of above-mentioned term in the present invention as the case may be.
Refering to fig. 1, a kind of Laboratory Waste Water Treatment equipment, sewage disposal system and the controller with display screen, sewage
Processing system according to sewage disposal sequence, be from upstream to downstream include pass sequentially through the connected sewage collecting pool 1 of pipeline, air supporting is stirred
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 equipped 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 on the air supporting stirring pool 5.
Pipeline between the air supporting stirring pool 5 and redox pond 6 is equipped with No. two elevator pumps 30.
The oxidation boost motor 36 being connected with controller is connected on the redox pond 6, oxidation boost motor 36 is oxidation
Restore the medicament that redox reaction is provided in pond.
Pipeline between the redox pond 6 and absorbent element is equipped with No. three elevator pumps 28.
The absorbent element be from upstream to downstream include the secondary absorption system 9 being sequentially connected, light electrolysis absorber 10,
Heavy metal adsorption device 11 and organic matter absorber 12.
The elevator pump 30, three of the No.1 elevator pump 34, two elevator pump 28, aerating pump 35 and 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 equipped in air supporting stirring pool 5.
Sewage disposal system further includes sludge drying device 33, and sludge drying device is equipped 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 sludge drying device 33 is equipped with one
Number mud valve 31 is connected with No. two mud valves on the pipeline between the mud inlet and redox pond 6 of the sludge drying device 33
29, the mud inlet of sludge drying device 33 is equipped with slush pump 32.
Sewage disposal system further includes cleaning system, and cleaning system includes 8, No. two cleaning pipes 20 and three of No.1 cleaning pipe
Number cleaning pipe 14；The No.1 cleaning pipe 8 is connected between water source 13 and secondary absorption system 9, and is connected in No.1 cleaning pipe 8
There is flushing valve 7；No. two cleaning pipes 20 are connected between water source 13 and biological reaction apparatus 21, and are connected in No. two cleaning pipes 20
There is backwash inlet valve 19；No. three cleaning pipes 14 are connected between water source 13 and biological reaction apparatus 21, and No. three cleaning pipes
It is connected on 14 and is just washing inlet valve 15.The both ends of biological reaction apparatus 21, which are respectively equipped with, just washes drainpipe 23 and backwash drainpipe 16；
It is just washing drainpipe 23 and is being equipped with positive valve 24, backwash drainpipe 16 is equipped with anti-valve 17；Just washing the flow of the discharge of drainpipe 23
To just washing collecting tank 25, the flow that backwash drainpipe 16 is discharged is to backwash collecting tank 18；Just washing collecting tank 25 and backwash collecting tank
Water in 18 is recovered in sewage collecting pool 1.
Pipeline between biological reaction apparatus 21 and photochemical catalytic oxidation system 26 is equipped with production water valve 22.
The secondary absorption of secondary absorption system 9 is respectively activated carbon adsorption and quartz sand absorption.
It is equipped with the conductance probe head being connected with controller in redox pond 6 and in photochemical catalytic oxidation system 26.
The controller is PLC or microcontroller.
The utility model is described further with reference to operation principle：
Sewage enters sewage collecting pool 1, then in turn through air supporting stirring pool 5, redox pond 6, absorbent element, life
Object reaction unit 21 and photochemical catalytic oxidation system 26, sewage is after the processing of final step photochemical catalytic oxidation system 26, flow direction
Drainage system 27.
When sewage enters when sewage collecting pool 1 is located at low liquid level or air supporting stirring pool 5 is located at high liquid 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 liquid level, No. two elevator pumps 30 stop
Only work.When redox pond 6 is located at low liquid level, No. three elevator pumps 28 are stopped.Sewage collecting pool 1 is interior, air supporting is stirred
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 passes through alkali case 2 and the alkalinity that alkali is adjusted to setting is added, then pass through PAC casees 4
PAC is added and carries out flocculation sediment, acid is then added by sour case 3 and is 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 is added medicament and is controlled by controller.
Sewage passes through secondary absorption system 9, light electrolysis absorber 10, a huge sum of money successively after oxidization-reduction pond 6 is handled
The adsorption treatment for belonging to 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 cleaning system timing.In cleaning system
Water source 13 is municipal water sources.When opening flushing valve 7, the water in water source 13 flows into secondary absorption system 9 by No.1 cleaning pipe 8,
Secondary absorption system 9 is cleaned.When opening backwash inlet valve 19 and anti-valve 17, the water at water source 13 passes through No. two cleaning pipes
20 enter biological reaction apparatus 21, are backwashed to biological reaction apparatus 21, and the water after backwash flows into instead from backwash drainpipe 16
Wash collecting tank 18.When opening is just washing inlet valve 15 and positive valve 24, the water in water source 13 flows into biology by No. three cleaning pipes 14
Reaction unit 21 is just rinsing biological reaction apparatus 21, and the water after positive flushing is flowed out from drainpipe 23 is just washed, and is entered and just washed
Collecting tank 25.
The utility model the qualified discharge water discharged in the waste water of collection, processing procedure, after having handled can be carried out pH,
Conductivity, turbidity are monitored on-line.Separately there is exceeded setting to manage：Setting allows to discharge supplemental characteristic alarm limits, such as discharges
Parameter values are more than setting limit value, remote monitoring system and host service function main interface meeting automatic alarm and show exceeded parameter, are controlled
Device processed starts limiting emission program, while starting overstandard waste water and carrying out reflow treatment program, and tracks and records, up to standard until handling
It afterwards just can automatic-discharging.
The utility model can be directed to the waste water of various concentration index, oneself adjust its dosing reaction time, whole process
Full automatic treatment waste water, ingredient and concentration for different waste water, then controller carries out calculating automatically to carry out automatically in proportion
Launch drug.
The utility model controller using Siemens's programmable logic controller (PLC) (PLC) complete electrically and meter section oneself
Dynamic control and monitoring, equipment is automatically controlled when 10 inches of Delta LCD liquid crystal touch screens Chinese displays can realize interactive mode, booting
System detects automatically.Interactive mode, data display management may be implemented：Liquid crystal display each unit operating status is digitized,
Such as cartoon type flow chart or with table, block diagram or trend diagram form show each processing unit liquid level, flow, hydraulic pressure, temperature,
The real-time running datas of the components such as voltage, electric current, anti-corrosion elevator pump, instrument and meter, monitoring device, historical data, alert data,
Operating status, running rate statistics, discharge capacity.
The utility model has medicine-chest medicament and exhausts prompt facility, and can be out of service after medicament exhausts, in addition medicine
After agent, can just it continue to run with.Each drip for ensureing to be discharged into city planting ductwork is handled by qualification.
The foregoing is merely specific embodiment of the utility model, but the technical characteristics of the utility model is not limited to
This, any those skilled in the art in the field of the utility model, made by changes or modifications all cover it is new in this practicality
Among the scope of the claims of type.
Claims (8)
1. a kind of Laboratory Waste Water Treatment equipment, it is characterized in that：Sewage disposal system and controller with display screen, at sewage
For reason system according to sewage disposal sequence, it includes passing sequentially through the connected sewage collecting pool of pipeline, air supporting stirring to be from upstream to downstream
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 equipped with No.1 elevator pump and dosing tank group, dosing tank group packet
Include alkali case, sour case and PAC casees；
Aerating pump is connected on the air supporting stirring pool；
Pipeline between the air supporting stirring pool and redox pond is equipped with No. two elevator pumps；
It is connected with oxidation boost motor on the redox pond；
Pipeline between the redox pond and absorbent element is equipped with No. three elevator pumps；
It includes the secondary absorption system being sequentially connected, light electrolysis absorber, heavy metal that the absorbent element, which is from upstream to downstream,
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；In sewage collecting pool, in dosing tank group, be equipped in air supporting stirring pool and redox pond and to be connected with controller
Liquid level sensor；The acidity-basicity sensor being connected with controller is equipped in 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 further includes dirt
Mud drying device, sludge drying device are equipped 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 sludge drying
Pipeline between the mud inlet and air supporting stirring pool of device is equipped with No.1 mud valve, the mud inlet and oxygen of the sludge drying device
Change and is connected with No. two mud valves on the pipeline between reduction pond.
3. a kind of Laboratory Waste Water Treatment equipment according to claim 1, it is characterized in that：Sewage disposal system further includes clear
System is washed, cleaning 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 in No.1 cleaning pipe；No. two cleaning pipes are connected to water source and biology
Between reaction unit, and backwash inlet valve is connected in No. two cleaning pipes；No. three cleaning pipes are connected to water source and biological respinse
Between device, and it is connected in No. three cleaning pipes and just washes inlet 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
Drainpipe and backwash drainpipe She You not just be washed；It is just washing drainpipe and is being equipped with positive valve, backwash drainpipe is equipped 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 equipped 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 activated carbon adsorption 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 in 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 microcontroller.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721729178.5U CN207699417U (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 |
|---|---|---|---|
| CN201721729178.5U CN207699417U (en) | 2017-12-12 | 2017-12-12 | A kind of Laboratory Waste Water Treatment equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207699417U true CN207699417U (en) | 2018-08-07 |
Family
ID=63025917
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721729178.5U Active CN207699417U (en) | 2017-12-12 | 2017-12-12 | A kind of Laboratory Waste Water Treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207699417U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107857442A (en) * | 2017-12-12 | 2018-03-30 | 四川卓越水处理设备有限公司 | A kind of Laboratory Waste Water Treatment equipment |
| 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 |
-
2017
- 2017-12-12 CN CN201721729178.5U patent/CN207699417U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107857442A (en) * | 2017-12-12 | 2018-03-30 | 四川卓越水处理设备有限公司 | A kind of Laboratory Waste Water Treatment equipment |
| 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 |
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Effective date of registration: 20240122 Address after: Floor 1-5, No.89-502, Huxian West Second Road, Pengzhou Industrial Development Zone, Chengdu, Sichuan 610000 Patentee after: Sichuan Zhuoshuiyue Medical Technology Co.,Ltd. Country or region after: China Address before: 610000 No. 99-11, West Avenue, West District, hi tech Zone, Chengdu, Sichuan Patentee before: SICHUAN EXCELLENT WATER TREATMENT EQUIPMENT Co.,Ltd. Country or region before: China |
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