CN106396270A - High-concentration pharmaceutical wastewater treatment system and treatment method - Google Patents
High-concentration pharmaceutical wastewater treatment system and treatment method Download PDFInfo
- Publication number
- CN106396270A CN106396270A CN201610947854.XA CN201610947854A CN106396270A CN 106396270 A CN106396270 A CN 106396270A CN 201610947854 A CN201610947854 A CN 201610947854A CN 106396270 A CN106396270 A CN 106396270A
- Authority
- CN
- China
- Prior art keywords
- equipment
- waste water
- tank
- water
- ozone
- 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
- 238000000034 method Methods 0.000 title claims abstract description 48
- 238000004065 wastewater treatment Methods 0.000 title abstract description 12
- 239000002351 wastewater Substances 0.000 claims abstract description 67
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 67
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 38
- 230000003647 oxidation Effects 0.000 claims abstract description 37
- 239000012528 membrane Substances 0.000 claims abstract description 30
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 29
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 18
- 238000004062 sedimentation Methods 0.000 claims abstract description 16
- 239000003344 environmental pollutant Substances 0.000 claims abstract description 12
- 231100000719 pollutant Toxicity 0.000 claims abstract description 12
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 11
- 238000006243 chemical reaction Methods 0.000 claims abstract description 10
- 238000004519 manufacturing process Methods 0.000 claims abstract description 5
- 239000010802 sludge Substances 0.000 claims abstract description 5
- 238000003860 storage Methods 0.000 claims abstract description 4
- 238000007790 scraping Methods 0.000 claims abstract description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 16
- 230000001954 sterilising effect Effects 0.000 claims description 14
- 230000005484 gravity Effects 0.000 claims description 12
- 230000000694 effects Effects 0.000 claims description 11
- 239000000126 substance Substances 0.000 claims description 11
- 239000003814 drug Substances 0.000 claims description 9
- 239000000377 silicon dioxide Substances 0.000 claims description 8
- 230000037452 priming Effects 0.000 claims description 7
- 239000000758 substrate Substances 0.000 claims description 7
- 238000003487 electrochemical reaction Methods 0.000 claims description 6
- 239000007788 liquid Substances 0.000 claims description 6
- 238000003672 processing method Methods 0.000 claims description 6
- 239000006228 supernatant Substances 0.000 claims description 6
- 239000000725 suspension Substances 0.000 claims description 6
- 238000005273 aeration Methods 0.000 claims description 5
- 239000012535 impurity Substances 0.000 claims description 5
- 239000008213 purified water Substances 0.000 claims description 5
- 239000005708 Sodium hypochlorite Substances 0.000 claims description 4
- 230000015556 catabolic process Effects 0.000 claims description 4
- 238000006731 degradation reaction Methods 0.000 claims description 4
- QWPPOHNGKGFGJK-UHFFFAOYSA-N hypochlorous acid Chemical compound ClO QWPPOHNGKGFGJK-UHFFFAOYSA-N 0.000 claims description 4
- 239000002893 slag Substances 0.000 claims description 4
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 claims description 4
- 241000700605 Viruses Species 0.000 claims description 3
- 238000004176 ammonification Methods 0.000 claims description 3
- 239000010405 anode material Substances 0.000 claims description 3
- 230000003197 catalytic effect Effects 0.000 claims description 3
- 230000009189 diving Effects 0.000 claims description 3
- 230000005684 electric field Effects 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- 229910021645 metal ion Inorganic materials 0.000 claims description 3
- 244000000010 microbial pathogen Species 0.000 claims description 3
- 238000006396 nitration reaction Methods 0.000 claims description 3
- 239000013618 particulate matter Substances 0.000 claims description 3
- 238000010992 reflux Methods 0.000 claims description 3
- 239000000356 contaminant Substances 0.000 claims description 2
- 150000003384 small molecules Chemical class 0.000 claims 1
- 239000004615 ingredient Substances 0.000 abstract 2
- 239000002699 waste material Substances 0.000 abstract 1
- 238000005516 engineering process Methods 0.000 description 20
- 239000000047 product Substances 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 201000010099 disease Diseases 0.000 description 3
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 231100000614 poison Toxicity 0.000 description 3
- 238000002306 biochemical method Methods 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 230000010354 integration Effects 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002574 poison Substances 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 206010002660 Anoxia Diseases 0.000 description 1
- 241000976983 Anoxia Species 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- 230000007953 anoxia Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 210000005056 cell body Anatomy 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000006056 electrooxidation reaction Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 230000001473 noxious effect Effects 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000009280 upflow anaerobic sludge blanket technology Methods 0.000 description 1
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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- 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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
- C02F1/4672—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
-
- 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
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
-
- 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
-
- 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
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- 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
- C02F2103/34—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
- C02F2103/343—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the pharmaceutical industry, e.g. containing antibiotics
-
- 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
- C02F3/02—Aerobic processes
-
- 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
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1236—Particular type of activated sludge installations
- C02F3/1268—Membrane bioreactor systems
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)
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The invention discloses a high-concentration pharmaceutical wastewater treatment system. The system comprises a pharmaceutical production wastewater collecting well, a grille waste remover, a comprehensive adjusting tank, electrocatalytic oxidation equipment, a vertical flow sedimentation tank, a first middle tank, an ozone oxidation tower, a second middle tank, a pre-reaction tank, an MBR membrane tank, a disinfection tank and ultrafiltration membrane equipment which are connected sequentially, water treated by the ultrafiltration membrane equipment enters a recycled water tank or is subjected to up-to-standard emission, a residue scraping equipment pipeline of the electrocatalytic oxidation equipment is connected with a dross tank, and sludge discharge pipelines of the vertical flow sedimentation tank and the MBR membrane tank are connected with a sludge storage tank. The invention further provides a treatment method of the high-concentration pharmaceutical wastewater treatment system. With the adoption of the high-concentration pharmaceutical wastewater treatment system and the treatment method, highly refractory pollutant ingredients are effectively degraded, and various ingredients in wastewater are effectively separated and reduced by the aid of local integrated equipment, so that the working efficiency and stability of the whole process are improved.
Description
Technical field
The present invention relates to high-concentration sewage disposal technology field, particularly belong to a kind of high concentration medical wastewater processing system and
Processing method.
Background technology
In many research of existing pharmaceutical wastewater treatment process and technology as can be seen that using single treatment technology,
Technique (biological treatment, physical treatment, any one in chemical treatment), has very to the effective process of high concentration medical wastewater
Big limitation." the omnipotent handling process-biological treatment " that some experts and scholars propose is in the face of most of high concentrated organic wastewaters
Process at all cannot ensure process after water outlet qualified discharge, therefore, how to select technique treatment in accordance with local conditions, pointedly set
Meter and research and development new technology, new technique are particularly important to current extremely severe environments situation.In recent years many studies have shown that, can
By, in the stain disease handling process that constitutes in biological processing unit, corresponding link being directed to dissimilar, variable concentrations
It is an effective method that pollutant carry out hierarchical segmented formula to remove.According to research reports, high-level oxidation technology and life
Being used in combination of thing treatment technology early has application, technology relative maturity in high concentration wastewater treatment field, but treatment effect is passed judgement on
Differ.At present, the most frequently used way is to adopt Fenton oxidation technology, H in pretreatment unit2O2Oxidation technology, ozone oxidation skill
Art, electrochemical oxidation technology, BAF and UASB technology and biologic treating technique are used in combination, and to be realized with this
Removal to hardly degraded organic substance and reduction.But as using which kind of advanced oxidation or which plant high-level oxidation technology with
Biological treatment combines, and where be combined but become the critical limitation of this kind of method popularization and application because
Element, defect present in prior art below：
(1) the pharmacy wastewater treatment technology based on Biochemical method is primarily present and need to add additional carbon, to high concentration
The biodegradability of hardly degraded organic substance is poor, system anti-pollution thing load impact ability is weak, longtime running system is unstable, process consumption
The shortcomings of duration, poor processing effect；
(2) Biochemical method technological process length, technique floor space be big, each section of civil engineering structure cell body is effectively sharp in technique
With rate is low, capital expenditure high cost the shortcomings of；
(3) traditional anaerobic-aerobic treatment technique to high-concentration hardly-degradable complexity organic pollution only carry out simple anaerobism,
Anoxia and Aerobic Process for Treatment, because stain disease processes microorganism itself anti-external environment high density pollution load impact adaptability difference
Many reasons, it fundamentally cannot realize safely and effectively degrading to numerous pollutant；
(4) poisonous and harmful substance containing in waste water can poison the numerous microorganisms in biological treatment, meeting when serious
The irreversibility causing processing system is destroyed, and the noxious substance containing in its water outlet can bring serious threat to receiving water body；
(5) in pharmacy waste water, pollutant load is high, complicated component, and it is automatic for single biochemistry and materializing strategy Technology
Change degree is relatively low, treatment effect is relatively poor, if a certain link goes wrong, all will be difficult to reach for whole system
Purpose to waste water final process and purification.
In sum, the prior art for pharmacy wastewater treatment is implicitly present in many being difficult to so that this technology is widely popularized
The defect of application, anxious to be resolved.
Content of the invention
The purpose of the present invention is to provide a kind of high concentration medical wastewater processing system and processing method, to reach to height
Recalcitrant chemicals composition is effectively degraded, and realize various composition in waste water efficiently separated by local integration apparatus and
Cut down, thus improve the work efficiency of whole PROCESS FOR TREATMENT and the purpose of stability.
A kind of high concentration medical wastewater processing system provided by the present invention is it is characterised in that include the system being sequentially connected
Medicine produce waste water sump, grid sewage-removing machine, comprehensive adjustment pond, electrocatalytic oxidation equipment, vertical sedimentation tank, the first intermediate pool,
Ozone oxidation tower, the second intermediate pool, pre-reaction pond, MBR membrane cisterna, sterilization pool, device for ultrafiltration membrane, after processing through device for ultrafiltration membrane
Water enters reuse pool or qualified discharge, and wherein, the slag equipment pipeline of scraping in electrocatalytic oxidation equipment connects scum silica frost pond, erects stream
The mud line of sedimentation tank and MBR membrane cisterna connects storage basin respectively.
Further, described sterilization pool is disappeared by connected sodium hypochlorite medicine machine and ozone devices
Poison.
Further, described reuse pool connects frequency-conversion water supply system.
Further, the system is additionally provided with auxiliary equipment, and described auxiliary equipment includes diving mixer, aeration wind
Machine, sludge reflux pump, product water self priming pump, backwash centrifugal pump and hypochlorous acid medicine machine.
Further, the system is managed equipment by PLC automation control system to system and is realized programme-control.
A kind of processing method based on high concentration medical wastewater processing system provided by the present invention is it is characterised in that make
The waste water that medicine produces removes oarse-grained suspension through grid sewage-removing machine by waste water sump evenly in grid sewage-removing machine
Property impurity, then remove through its fine fack after tiny particulate contaminants substrate, water outlet gravity flow enters in comprehensive adjustment pond, waste water
In the tiny suspension particulate matter carried secretly, be gradually deposited at comprehensive adjustment at the bottom of pond portion, waste water quality and the water yield all obtain all with.This
Afterwards, by one-level elevator pump, waste water is equably promoted in electrocatalytic oxidation equipment, the organic pollution in this stage waste water
Common participation electrochemical reaction process, the most of difficult degradation macromole in the presence of external dc power supply, in waste water solution
Organic substance is gradually degraded, and the flco class material producing in electrochemical reaction process will be in the presence of electric field, with anode material
Expect the Al being electrolysed out3+、Fe3+Deng metal ion, form stable complex, a part of complex is countless by produced by negative electrode
H2、O2Micro-bubble takes liquid surface to, and by the scum silica frost doctoring apparatus above electrocatalytic oxidation equipment, scraped drain into floating
In slag bath, another part complex will be gradually deposited at electrocatalytic oxidation device bottom, can be by periodically turning on the shape of mud valve
Formula, removes it, the supernatant after processing through electrocatalytic oxidation equipment, and water outlet gravity flow enters vertical sedimentation tank, partly not yet in effect
The cotton-shaped complex of sedimentation will be deposited in sedimentation tank bottom under gravity, and supernatant then flows automatically in the middle of entrance first
Pond, by two-stage hoisting pump by clarify after waste water solution be promoted in ozone oxidation tower, enter tower in waste water solution through with smelly
The ozone that Oxygen Generator produces, by the air-water contact equipment within ozone oxidation tower, ozone and waste water is fully mixed
Splice grafting touches, and the hardly degraded organic substance in waste water is fully degraded to degradable little point by Strong oxdiative feature using ozone further
Sub- Organic substance, is greatly improved the biodegradability of waste water, and water outlet enters pre-reaction pond after the second intermediate pool, in facultative microbe
Under collective effect, realize the degraded further to Wastewater Pollutant substrate and removal, water outlet gravity flow enters in MBR membrane cisterna, good
Oxygen animalcule, including under ammonifiers, the comprehensive function of nitrifier, carries out ammonification, nitration reaction, then through MBR membrane module realization at
Purified water after reason is efficiently separated with pollutant impurity, and water outlet after treatment flows through sterilization pool, in ozone and hypochlorous
Under collective effect, kill the pathogenic microorganism in water outlet and virus, the water outlet after sterilization is promoted to ultrafilter membrane through three-level elevator pump
In equipment, carry out final deep purifying and process, to guarantee the final security and stability of water outlet after processing, until meeting row up to standard
Put or flow into utilization to be recycled in reuse pool.
A kind of high concentration medical wastewater processing system provided by the present invention and processing method, employ materializing strategy and life
The handling process that change process combines, is different from and is related to single Strong oxdiative technology, electrocatalytic oxidation in other handling processes
Technology, MBR membrane technology etc., because of its complicated component and containing certain for the pharmacy class wastewater treatment of highly difficult degraded
Bio-toxicity, is only difficult to it by single high-level oxidation technology or biochemical processing and effectively degrades, logical in the present invention
Cross and above technology is carried out rational combination application, give full play to the technical advantage of different disposal section, process from whole stain disease
From the point of view of flow process, this technique achieves hierarchical classification time and processes to the pollutant substrate in pharmacy waste water, not only can be to high difficult degradation
Pollutant component carries out degraded and can also realize efficiently separating and cutting down to phase each in waste water by local integration apparatus.Separately
Outward, programme-control is realized to each processing equipment of system by PLC automation control system so that system manages equipment room
Coordinated operation harmony and stability all can be protected, in sum, the present invention to high concentration medical wastewater treatment effeciency and
The lifting aspect of whole processing system stability has significant technical advantage.
Brief description
Fig. 1 is the technological process of production schematic diagram of the present invention.
Specific embodiment
With specific embodiment, the present invention is described in further detail below in conjunction with the accompanying drawings：
As shown in figure 1, a kind of high concentration medical wastewater processing system provided by the present invention, including the pharmacy being sequentially connected
Produce waste water sump, grid sewage-removing machine, comprehensive adjustment pond, electrocatalytic oxidation equipment, vertical sedimentation tank, the first intermediate pool,
Ozone oxidation tower, the second intermediate pool, pre-reaction pond, MBR membrane cisterna, sterilization pool (ozone and hypochlorous acid sterilization), device for ultrafiltration membrane, warp
Water after device for ultrafiltration membrane is processed enters reuse pool or qualified discharge, reuse pool, wherein, in electrocatalytic oxidation equipment
Scrape slag equipment pipeline and connect scum silica frost pond, the mud line of described vertical sedimentation tank and MBR membrane cisterna connects storage basin respectively.Described
Sterilization pool carried out disinfection by connected sodium hypochlorite medicine machine and ozone devices.Additionally, described recycle-water
Pond connects frequency-conversion water supply system.Additionally, the auxiliary equipment of the present invention also include diving mixer, Aeration fan, sludge reflux pump,
Produce water self priming pump, backwash centrifugal pump and hypochlorous acid medicine machine.
The present invention realizes programme-control by PLC automation control system to each processing equipment.Its concrete operating principle is such as
Under：Enter the PLC control system page, display system automatic running and system run two kinds of operational modes manually, click on system certainly
Dynamic button, whole Waste Water Treatment enters automatic running pattern.Grid sewage-removing machine realizes intermittent operation under PLC effect,
Now one-level elevator pump brings into operation and supplies water to electrocatalytic oxidation equipment, and electrocatalytic oxidation equipment is started working, when comprehensive tune
When section pond is in low liquid level, in addition to Aeration fan time delay runs, other equipment is all out of service；Treat that water level returns to normal level
After level time delay 10 minutes, Waste Water Treatment is again introduced into normal operating condition.Water outlet enters in the middle of first after precipitation
Pond by two-stage hoisting pump, carries out Strong oxdiative process by inside waste water lifting to ozone catalytic tower, at the first middle pool water level
In back segment equipment when low liquid level in addition to Aeration fan time delay operation, other equipment is all out of service, treats that water level returns to normally
After fluid level, time delay entered normal operating condition after 10 minutes.Water outlet sequentially passes through the second intermediate pool, pretreatment pool and MBR
Membrane cisterna, realizes the product water process of its purified water by the continuous alternate run work of two product water self priming pumps in MBR membrane cisterna,
During produce water self priming pump start and stop controlled by PLC internal processes, in the present embodiment, every product water pump operation 8min, stop
Have a rest 2min, and every two product water self priming pumps of 120min carry out rotation.In addition, water level exceedes high level in MBR membrane cisterna, then one-level lifting
Pump is automatically stopped operation, and other equipment is normally run, and after the level to normal level to be restored, time delay enters normal fortune after 10 minutes
Row state, in MBR membrane cisterna water level be less than protection liquid level when two produce water self priming pumps all quit work, to be restored to normal level water
After flat, time delay entered normal operating condition after 10 minutes.Sterilization pool passes through connected sodium hypochlorite medicine machine and smelly
Purified water after oxygen equipment disinfection is promoted in device for ultrafiltration membrane further through three-level elevator pump and is processed, finally
A part of water outlet is stored in reuse pool, and another part standard water discharge is discharged.
Specifically, when needing a certain local devices are operated, after entrance system, click system is automatically stopped
Button, ends with system automatic running pattern, then pass through click system hand push button, enter system manual mode of operation, according to need
Will, specifically Non-follow control can be carried out to a certain or multiple devices, specifically enter operation pages click corresponding device startup and press
Button can achieve.
It is below the technological process of production of the present invention：The waste water of pharmaceutical manufacturing is by waste water sump evenly into grid
In spotter, remove oarse-grained suspension impurity through grid sewage-removing machine, then remove tiny graininess pollution through its fine fack
After thing substrate, water outlet gravity flow enters in comprehensive adjustment pond, and the tiny suspension particulate matter carried secretly in waste water is gradually deposited at synthesis
Regulating reservoir bottom, waste water quality and the water yield all obtain all with.Hereafter, by one-level elevator pump, waste water is equably promoted to electricity
In oxidation equipment, the organic pollution in this stage waste water participates in electrochemical reaction process, jointly in external dc power supply
In the presence of, the most of difficult degradation larger molecular organicses in waste water waste water solution are gradually degraded, in electrochemical reaction process
The flco class material producing will be in the presence of electric field, the Al that is electrolysed out with anode material3+、Fe3+Deng metal ion, formed
Stable complex, the countless H that a part of complex will be produced by negative electrode2、O2Micro-bubble takes liquid surface to, and by electricity
Scum silica frost doctoring apparatus above oxidation equipment, are scraped and are drained in scum silica frost pond, another part complex will be gradually deposited at
Electrocatalytic oxidation device bottom, can be removed it by periodically turning on the form of mud valve, after processing through electrocatalytic oxidation equipment
Supernatant, water outlet gravity flow enters vertical sedimentation tank, and partly the cotton-shaped complex of sedimentation not yet in effect will be under gravity heavy
Shallow lake at the bottom of pond portion is deposited, and supernatant then flows automatically and enters the first intermediate pool, is carried the waste water solution after clarifying by two-stage hoisting pump
Rise in ozone oxidation tower, enter the ozone that the waste water solution warp in tower is produced with ozonator, by ozone catalytic tower
The air-water contact equipment in portion, ozone and waste water are carried out being sufficiently mixed contacting, using ozone Strong oxdiative feature by waste water
Hardly degraded organic substance be fully degraded to degradable small organic molecule further, the biodegradability of waste water is greatly improved, goes out
Water enters pre-reaction pond after the second intermediate pool, under the collective effect of facultative microbe, realizes to Wastewater Pollutant substrate
Degrade further and remove, water outlet gravity flow enters in MBR membrane cisterna, in aerobic microbiological, the synthesis including ammonifiers, nitrifier is made
With under, carry out ammonification, nitration reaction, then the efficiently separating of the purified water after processing and pollutant impurity through MBR membrane module realization,
Water outlet after treatment flows through sterilization pool, under ozone and hypochlorous collective effect, kill water outlet in pathogenic microorganism and
Virus, the water outlet after sterilization is promoted in device for ultrafiltration membrane through three-level elevator pump, carries out final deep purifying and processes, to guarantee
The final security and stability of water outlet after process, until meeting qualified discharge or flowing into utilization to be recycled in reuse pool.
Claims (6)
1. a kind of high concentration medical wastewater processing system it is characterised in that include be sequentially connected pharmacy wastewater sump,
Grid sewage-removing machine, comprehensive adjustment pond, electrocatalytic oxidation equipment, vertical sedimentation tank, the first intermediate pool, ozone oxidation tower, in second
Between pond, pre-reaction pond, MBR membrane cisterna, sterilization pool, device for ultrafiltration membrane, through device for ultrafiltration membrane process after water enter reuse pool or
Person's qualified discharge, wherein, the slag equipment pipeline of scraping in electrocatalytic oxidation equipment connects scum silica frost pond, vertical sedimentation tank and MBR film
The mud line in pond connects storage basin respectively.
2. high concentration medical wastewater processing system according to claim 1 it is characterised in that described sterilization pool by with
Its sodium hypochlorite medicine machine connecting and ozone devices carry out disinfection.
3. high concentration medical wastewater processing system according to claim 1 is it is characterised in that described reuse pool connects
Frequency-conversion water supply system.
4. high concentration medical wastewater processing system according to claim 1 is it is characterised in that the system is additionally provided with auxiliary
Equipment, described auxiliary equipment include diving mixer, Aeration fan, sludge reflux pump, produce water self priming pump, backwash centrifugal pump and
Hypochlorous acid medicine machine.
5. high concentration medical wastewater processing system according to claim 1 is it is characterised in that the system is automatic by PLC
Networked control systems realize programme-control to system reason equipment.
6. the processing method of high concentration medical wastewater processing system according to claim 1 is it is characterised in that pharmaceutical manufacturing
Waste water by waste water sump evenly in grid sewage-removing machine, remove oarse-grained suspension through grid sewage-removing machine miscellaneous
Matter, then remove through its fine fack after tiny particulate contaminants substrate, water outlet gravity flow enters in comprehensive adjustment pond, presss from both sides in waste water
The tiny suspension particulate matter of band, is gradually deposited at comprehensive adjustment at the bottom of pond portion, waste water quality and the water yield all obtain all with；Hereafter,
By one-level elevator pump, waste water is equably promoted in electrocatalytic oxidation equipment, the organic pollution in this stage waste water is altogether
With participating in electrochemical reaction process, in the presence of external dc power supply, the most of difficult degradation macromole in waste water solution has
Machine thing is gradually degraded, and the flco class material producing in electrochemical reaction process will be in the presence of electric field, with anode material
The Al being electrolysed out3+、Fe3+Deng metal ion, form stable complex, the countless H that a part of complex will be produced by negative electrode2、
O2Micro-bubble takes liquid surface to, and by the scum silica frost doctoring apparatus above electrocatalytic oxidation equipment, is scraped and drain into scum silica frost
Chi Zhong, another part complex will be gradually deposited at electrocatalytic oxidation device bottom, can by periodically turning on the form of mud valve,
Remove it, the supernatant after processing through electrocatalytic oxidation equipment, water outlet gravity flow enters vertical sedimentation tank, partly sedimentation not yet in effect
Cotton-shaped complex will be deposited in sedimentation tank bottom under gravity, supernatant then flow automatically entrance the first intermediate pool, by
Waste water solution after clarifying is promoted in ozone oxidation tower two-stage hoisting pump, and the waste water solution warp entering in tower is occurred with ozone
The ozone that device produces, by the air-water contact equipment within ozone catalytic tower, ozone and waste water is carried out being sufficiently mixed contacting,
Hardly degraded organic substance in waste water is fully degraded to further degradable small molecule using the Strong oxdiative feature of ozone organic
Thing, is greatly improved the biodegradability of waste water, and water outlet enters pre-reaction pond after the second intermediate pool, in the common work of facultative microbe
With under, realize to the degraded further of Wastewater Pollutant substrate and removal, water outlet gravity flow enters in MBR membrane cisterna, in aerobic micro- life
Thing, including under ammonifiers, the comprehensive function of nitrifier, carries out ammonification, nitration reaction, then after MBR membrane module realization process
Purified water is efficiently separated with pollutant impurity, and water outlet after treatment flows through sterilization pool, in ozone and hypochlorous common work
With under, kill the pathogenic microorganism in water outlet and virus, the water outlet after sterilization is promoted in device for ultrafiltration membrane through three-level elevator pump,
Carry out final deep purifying to process, to guarantee the final security and stability of water outlet after processing, until meet qualified discharge or
Flow into utilization to be recycled in reuse pool.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610947854.XA CN106396270A (en) | 2016-10-26 | 2016-10-26 | High-concentration pharmaceutical wastewater treatment system and treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610947854.XA CN106396270A (en) | 2016-10-26 | 2016-10-26 | High-concentration pharmaceutical wastewater treatment system and treatment method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106396270A true CN106396270A (en) | 2017-02-15 |
Family
ID=58014007
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610947854.XA Pending CN106396270A (en) | 2016-10-26 | 2016-10-26 | High-concentration pharmaceutical wastewater treatment system and treatment method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106396270A (en) |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107098513A (en) * | 2017-04-28 | 2017-08-29 | 浙江奇彩环境科技股份有限公司 | A kind of processing method of high concentration morpholine waste water |
| CN107365050A (en) * | 2017-07-17 | 2017-11-21 | 杭州尚杭科技有限公司 | The waste liquid electrolytic processing method of intelligent environment protection toilet |
| CN107792973A (en) * | 2017-12-01 | 2018-03-13 | 杭州民天环保技术研究所有限公司 | A kind of water treatment technology |
| CN108217784A (en) * | 2018-03-23 | 2018-06-29 | 南方创业（天津）科技发展有限公司 | The control system and method for sewage disposal device |
| CN108358395A (en) * | 2018-03-23 | 2018-08-03 | 大连大学 | A kind for the treatment of process of pesticide wastewater |
| CN108358386A (en) * | 2018-03-02 | 2018-08-03 | 成都知联汇科技有限公司 | A kind for the treatment of process of antibiotic pharmaceutical wastewater |
| CN108373237A (en) * | 2018-03-23 | 2018-08-07 | 大连大学 | A kind of processing unit of pesticide wastewater |
| CN109179882A (en) * | 2018-09-29 | 2019-01-11 | 云南滇清环境科技有限公司 | A kind of pharmacy waste water Treated sewage reusing processing system and method |
| CN109626761A (en) * | 2019-02-02 | 2019-04-16 | 河北科技大学 | The devices and methods therefor of catalytic ozonation joint MBR deep treatment of pharmaceutical waste water |
| CN111606507A (en) * | 2020-05-20 | 2020-09-01 | 苏州首创嘉净环保科技股份有限公司 | Integrated equipment for medical sewage disinfection treatment |
| CN113307420A (en) * | 2021-06-03 | 2021-08-27 | 赛恩斯环保股份有限公司 | Method for removing COD (chemical oxygen demand) in metallurgical wastewater |
| CN114956273A (en) * | 2022-04-12 | 2022-08-30 | 科盛环保科技股份有限公司 | Electrochemical treatment device and process for improving biodegradability of traditional Chinese medicine wastewater |
Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20050084921A1 (en) * | 2001-11-09 | 2005-04-21 | Cranley Paul E. | Enzyme-based system and sensor for measuring acetone |
| CN101428946A (en) * | 2008-12-02 | 2009-05-13 | 金荷英 | Integrated treatment process and equipment for domestic wastewater |
| CN101560040A (en) * | 2009-05-08 | 2009-10-21 | 北京清大国华环保科技有限公司 | Method and device for processing pharmaceutical wastewater by pulse electrocoagulation-MBR |
| CN101591121A (en) * | 2009-06-26 | 2009-12-02 | 东北大学 | The method of film biodegradation, hydrogen peroxide oxidation treating xanthate wastewater through combination |
| CN102336502A (en) * | 2011-08-26 | 2012-02-01 | 无锡通源环保技术工程有限公司 | Combination type treatment method for pharmaceutical waste water |
| CN103739124A (en) * | 2014-01-24 | 2014-04-23 | 太平洋水处理工程有限公司 | Efficient water treatment device and water treatment method |
| CN105417899A (en) * | 2016-01-13 | 2016-03-23 | 樊利华 | Ultrasonic electro-adsorption electro-Fenton and desalination and decoloration water treatment device and method |
| CN105585222A (en) * | 2016-02-26 | 2016-05-18 | 河南科技学院 | Chemical sewage treatment device |
| CN105923931A (en) * | 2016-07-12 | 2016-09-07 | 郑州大学综合设计研究院有限公司 | Process for advanced treatment of antibiotic waste water |
| CN106007184A (en) * | 2016-06-27 | 2016-10-12 | 江苏佳羽环境科技有限公司 | Pharmaceutical wastewater treatment system |
| CN206476856U (en) * | 2016-10-26 | 2017-09-08 | 云南炳森环境工程有限公司 | A kind of high concentration medical wastewater processing unit |
-
2016
- 2016-10-26 CN CN201610947854.XA patent/CN106396270A/en active Pending
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20050084921A1 (en) * | 2001-11-09 | 2005-04-21 | Cranley Paul E. | Enzyme-based system and sensor for measuring acetone |
| CN101428946A (en) * | 2008-12-02 | 2009-05-13 | 金荷英 | Integrated treatment process and equipment for domestic wastewater |
| CN101560040A (en) * | 2009-05-08 | 2009-10-21 | 北京清大国华环保科技有限公司 | Method and device for processing pharmaceutical wastewater by pulse electrocoagulation-MBR |
| CN101591121A (en) * | 2009-06-26 | 2009-12-02 | 东北大学 | The method of film biodegradation, hydrogen peroxide oxidation treating xanthate wastewater through combination |
| CN102336502A (en) * | 2011-08-26 | 2012-02-01 | 无锡通源环保技术工程有限公司 | Combination type treatment method for pharmaceutical waste water |
| CN103739124A (en) * | 2014-01-24 | 2014-04-23 | 太平洋水处理工程有限公司 | Efficient water treatment device and water treatment method |
| CN105417899A (en) * | 2016-01-13 | 2016-03-23 | 樊利华 | Ultrasonic electro-adsorption electro-Fenton and desalination and decoloration water treatment device and method |
| CN105585222A (en) * | 2016-02-26 | 2016-05-18 | 河南科技学院 | Chemical sewage treatment device |
| CN106007184A (en) * | 2016-06-27 | 2016-10-12 | 江苏佳羽环境科技有限公司 | Pharmaceutical wastewater treatment system |
| CN105923931A (en) * | 2016-07-12 | 2016-09-07 | 郑州大学综合设计研究院有限公司 | Process for advanced treatment of antibiotic waste water |
| CN206476856U (en) * | 2016-10-26 | 2017-09-08 | 云南炳森环境工程有限公司 | A kind of high concentration medical wastewater processing unit |
Cited By (17)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107098513B (en) * | 2017-04-28 | 2021-01-01 | 浙江奇彩环境科技股份有限公司 | Method for treating high-concentration morpholine wastewater |
| CN107098513A (en) * | 2017-04-28 | 2017-08-29 | 浙江奇彩环境科技股份有限公司 | A kind of processing method of high concentration morpholine waste water |
| CN107365050A (en) * | 2017-07-17 | 2017-11-21 | 杭州尚杭科技有限公司 | The waste liquid electrolytic processing method of intelligent environment protection toilet |
| CN107792973A (en) * | 2017-12-01 | 2018-03-13 | 杭州民天环保技术研究所有限公司 | A kind of water treatment technology |
| CN107792973B (en) * | 2017-12-01 | 2023-11-17 | 浙江环普新材料科技有限公司 | Water treatment process |
| CN108358386A (en) * | 2018-03-02 | 2018-08-03 | 成都知联汇科技有限公司 | A kind for the treatment of process of antibiotic pharmaceutical wastewater |
| CN108217784A (en) * | 2018-03-23 | 2018-06-29 | 南方创业（天津）科技发展有限公司 | The control system and method for sewage disposal device |
| CN108358395A (en) * | 2018-03-23 | 2018-08-03 | 大连大学 | A kind for the treatment of process of pesticide wastewater |
| CN108373237A (en) * | 2018-03-23 | 2018-08-07 | 大连大学 | A kind of processing unit of pesticide wastewater |
| CN108373237B (en) * | 2018-03-23 | 2020-09-22 | 大连大学 | Pesticide waste water's processing apparatus |
| CN109179882A (en) * | 2018-09-29 | 2019-01-11 | 云南滇清环境科技有限公司 | A kind of pharmacy waste water Treated sewage reusing processing system and method |
| CN109626761A (en) * | 2019-02-02 | 2019-04-16 | 河北科技大学 | The devices and methods therefor of catalytic ozonation joint MBR deep treatment of pharmaceutical waste water |
| CN111606507A (en) * | 2020-05-20 | 2020-09-01 | 苏州首创嘉净环保科技股份有限公司 | Integrated equipment for medical sewage disinfection treatment |
| CN113307420A (en) * | 2021-06-03 | 2021-08-27 | 赛恩斯环保股份有限公司 | Method for removing COD (chemical oxygen demand) in metallurgical wastewater |
| CN113307420B (en) * | 2021-06-03 | 2022-05-31 | 赛恩斯环保股份有限公司 | Method for removing COD (chemical oxygen demand) in metallurgical wastewater |
| CN114956273A (en) * | 2022-04-12 | 2022-08-30 | 科盛环保科技股份有限公司 | Electrochemical treatment device and process for improving biodegradability of traditional Chinese medicine wastewater |
| CN114956273B (en) * | 2022-04-12 | 2023-09-29 | 科盛环保科技股份有限公司 | Electrochemical treatment device and process for improving biodegradability of traditional Chinese medicine wastewater |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106396270A (en) | High-concentration pharmaceutical wastewater treatment system and treatment method | |
| CN110422964A (en) | A kind of chemical industrial park wastewater deep treatment process method | |
| CN102786182B (en) | Device for processing landfill leachate | |
| CN206476860U (en) | A kind of oily waste water treatment reclamation set | |
| CN105731724B (en) | A kind of offshore platform life sewage treatment and reuse method with high salt | |
| CN110713314A (en) | Method for treating landfill leachate | |
| KR100906742B1 (en) | Treatment method and the apparatus including ultasonic-electrolysis-precipitator and complexed upper filter isolator for domestic sewage or wasted water | |
| CN106116031A (en) | A kind of efficient treatment process of slaughtering wastewater | |
| CN107176760A (en) | A kind of high salt advance for the treatment of process of cyanide-bearing effluent and processing system | |
| CN109534601A (en) | A kind of biochemical method for combining electrocatalytic oxidation processing landfill leachate | |
| CN108503019A (en) | A kind of membrane bioreactor and sewage water treatment method | |
| CN109111019B (en) | Method and system for treating high-concentration and degradation-resistant chemical synthesis pharmaceutical wastewater | |
| CN104710077B (en) | The processing system of synthetic rubber waste water and its processing method | |
| CN113087314A (en) | Wastewater treatment system and treatment process | |
| JP2005169304A (en) | Method of treating high concentration colored organic waste water | |
| CN108675545A (en) | A kind for the treatment of process of civil engineering sanitary sewage | |
| JP2006312124A (en) | Sludge treatment method | |
| CN205590517U (en) | Ozone - membrane bioreactor coking wastewater advanced treatment unit that pH control was adjusted | |
| CN103910469B (en) | The treatment process of the brine waste that food-processing produces | |
| CN206476856U (en) | A kind of high concentration medical wastewater processing unit | |
| CN105130131A (en) | Treatment system and method of landfill refuse leachate | |
| CN205328795U (en) | Wet spinning acrylic fibres production polymerization effluent disposal system | |
| CN114409207A (en) | Printing ink effluent disposal system | |
| CN211226789U (en) | Hardly biodegradable organic wastewater treatment equipment | |
| CN204958650U (en) | Hydrolytic acidification -AO - deposits integration reaction tank |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20170215 |
|
| WD01 | Invention patent application deemed withdrawn after publication |