CN110498561A - A kind of processing system and processing method of glass cover-plate abrasive waste water - Google Patents
A kind of processing system and processing method of glass cover-plate abrasive waste water Download PDFInfo
- Publication number
- CN110498561A CN110498561A CN201910722267.4A CN201910722267A CN110498561A CN 110498561 A CN110498561 A CN 110498561A CN 201910722267 A CN201910722267 A CN 201910722267A CN 110498561 A CN110498561 A CN 110498561A
- Authority
- CN
- China
- Prior art keywords
- water
- waste water
- glass cover
- reuse
- tank
- 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
- 239000002351 wastewater Substances 0.000 title claims abstract description 115
- 239000011521 glass Substances 0.000 title claims abstract description 38
- 238000003672 processing method Methods 0.000 title claims abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 178
- 238000004062 sedimentation Methods 0.000 claims abstract description 34
- 239000010802 sludge Substances 0.000 claims abstract description 31
- 230000001112 coagulating effect Effects 0.000 claims abstract description 22
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 20
- 238000001764 infiltration Methods 0.000 claims abstract description 14
- 238000005202 decontamination Methods 0.000 claims abstract description 10
- 230000003588 decontaminative effect Effects 0.000 claims abstract description 10
- 230000035484 reaction time Effects 0.000 claims description 16
- 230000015271 coagulation Effects 0.000 claims description 15
- 238000005345 coagulation Methods 0.000 claims description 15
- 238000006243 chemical reaction Methods 0.000 claims description 13
- 238000005189 flocculation Methods 0.000 claims description 13
- 230000016615 flocculation Effects 0.000 claims description 13
- 230000003750 conditioning effect Effects 0.000 claims description 12
- 230000004907 flux Effects 0.000 claims description 12
- 239000002253 acid Substances 0.000 claims description 10
- 239000006228 supernatant Substances 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 8
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 claims description 5
- 238000010612 desalination reaction Methods 0.000 claims description 5
- 238000002347 injection Methods 0.000 claims description 5
- 239000007924 injection Substances 0.000 claims description 5
- 238000007906 compression Methods 0.000 claims description 4
- 230000000694 effects Effects 0.000 claims description 4
- 238000000227 grinding Methods 0.000 claims description 4
- 238000010992 reflux Methods 0.000 claims description 3
- 239000004568 cement Substances 0.000 claims description 2
- 230000035939 shock Effects 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 12
- 239000012528 membrane Substances 0.000 description 10
- 238000003801 milling Methods 0.000 description 9
- 239000010865 sewage Substances 0.000 description 6
- 241000220324 Pyrus Species 0.000 description 4
- 235000021017 pears Nutrition 0.000 description 4
- 230000000903 blocking effect Effects 0.000 description 3
- 238000001223 reverse osmosis Methods 0.000 description 3
- 238000004065 wastewater treatment Methods 0.000 description 3
- 241000894006 Bacteria Species 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000010797 grey water Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000001471 micro-filtration Methods 0.000 description 1
- 230000000116 mitigating effect Effects 0.000 description 1
- 239000010841 municipal wastewater Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 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
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- 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
- C02F1/52—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
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- 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
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
-
- 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
- C02F3/30—Aerobic and anaerobic processes
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)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
Abstract
The invention discloses a kind of processing systems of glass cover-plate abrasive waste water, including wastewater equalization pond, coagulating sedimentation system, activated Sludge System and the MBR system being sequentially communicated, the water outlet of the MBR system is communicated with the first reuse water collection system and/or the second reuse water collection system by connecting line；The first reuse water collection system includes decontamination system and the first recycle-water tank；The second reuse water collection system includes the ultrafiltration system being sequentially communicated, counter-infiltration system and the second recycle-water tank.The present invention also provides a kind of processing methods of glass cover-plate abrasive waste water.The processing system and processing method of glass cover-plate abrasive waste water of the invention have many advantages, such as that stable effluent quality, strong shock resistance, film service life are long.
Description
Technical field
The invention belongs to field of waste water treatment more particularly to the processing systems and processing method of a kind of abrasive waste water.
Background technique
Glass cover processing industry, grinding precision is high, and Water usage is big.Under ten, water Policy Backgrounds, waste water is carried out
Recycling processing technique is studied to reduce the discharge of waste water, and great lot of water resources is saved, and the pollution for mitigating environment is of great significance.
The prior art is mainly " materializing strategy+micro-filtration+UF+ to the processing of glass cover-plate abrasive waste water and Treated sewage reusing technique
RO " technique, treatment process are poor to the Treated sewage reusing adaptability of glass cover-plate abrasive waste water, are easy to cause ultrafiltration membrane by small
Grain milling and the blocking of PAM combination, and then reverse osmosis membrane is blocked, cause the intermediate water reuse system service life to greatly reduce, general film
Service life only 1-2.
Summary of the invention
The technical problem to be solved by the present invention is to overcome the shortcomings of to mention in background above technology and defect, one kind is provided
The processing system and processing method of the long glass cover-plate abrasive waste water of stable effluent quality, strong shock resistance, film service life.
In order to solve the above technical problems, technical solution proposed by the present invention are as follows:
A kind of processing system of glass cover-plate abrasive waste water, including be sequentially communicated wastewater equalization pond, coagulating sedimentation system,
The water outlet of activated Sludge System and MBR system, the MBR system is communicated with the first reuse water collection system by connecting line
And/or the second reuse water collection system；The first reuse water collection system includes decontamination system and the first recycle-water tank；
The second reuse water collection system includes the ultrafiltration system being sequentially communicated, counter-infiltration system and the second recycle-water tank.
In above-mentioned processing system, it is preferred that the coagulating sedimentation system includes pH conditioning tank, the coagulating being sequentially communicated
Pond is adjusted back in pond, flocculation tank, sedimentation basin and pH, and the coagulation reaction tank is equipped with PAC feed opening, on the flocculation tank
Equipped with PAM feed opening.
In above-mentioned processing system, it is preferred that be additionally provided with anoxic pond between the coagulating sedimentation system and activated Sludge System.
In above-mentioned processing system, it is preferred that the sludge reflux of the MBR system discharge to the anoxic pond.
As a general technical idea, the present invention also provides a kind of processing methods of glass cover-plate abrasive waste water, including
Following steps:
S1: it is pumped into coagulating sedimentation again after glass cover-plate abrasive waste water injection wastewater equalization pond to be adjusted to the water quality and quantity of waste water
System after dosing coagulating sedimentation, collects supernatant；
S2: supernatant is passed through into anoxic pond, activated Sludge System and MBR system, collects the water outlet of MBR system；
S3: being delivered to the first reuse water collection system and/or the second reuse water collection system for the water outlet of MBR system, defeated
When sending to the first reuse water collection system, the water outlet of MBR system flows into the first recycle-water tank after decontamination system；Conveying
When to the second reuse water collection system, the water outlet of MBR system successively flows into the second reuse after ultrafiltration system, counter-infiltration system
Water tank；When being delivered to the first reuse water collection system and the second reuse water collection system, the water outlet of MBR system is divided into two-way
The first reuse water collection system and the second reuse water collection system are inputted, respectively reaches the first recycle-water tank after treatment
With the second recycle-water tank.
In above-mentioned processing method, it is preferred that the glass cover-plate abrasive waste water adjusts the water of waste water by wastewater equalization pond
After matter water, COD 200-300mg/L, SS 2000-5000mg/L, ammonia nitrogen 10-20mg/L, conductivity 600-800
μs/cm。
In above-mentioned processing method, it is preferred that the coagulating sedimentation system includes pH conditioning tank, the coagulating being sequentially communicated
Pond, flocculation tank, sedimentation basin and pH adjust back pond, and reaction time of the waste water in pH conditioning tank is 10-30min, and is added
The pH value for entering acid/base control waste water is 8-9；Reaction time of the waste water in coagulation reaction tank is 10-30min, and is added
The PAC of 100-200mg/L is handled；Reaction time of the waste water in flocculation tank is 10-30min, and 0.5- is added
The PAM of 2mg/L is handled；Sedimentation time of the waste water in sedimentation basin is not less than 2h, and surface loading is controlled in 0.8m3/(m2·
H) below；Reaction time of the waste water in pH readjustment pond is 10-30min, and the pH value that acid control waste water is added is 6.8-
7.2。
In above-mentioned processing method, it is preferred that residence time 6-10h of the waste water in activated Sludge System, control are lived
Property sludge system in DO content 3.0-3.5mg/L, activated sludge content be 3000mg/L；The waste water stops in MBR system
Staying the time is 2h, and permeant flux is in 12-15L/ (m2·h)。
In above-mentioned processing method, it is preferred that when ultrafiltration system processing, water production control flux is 40-50L/ (m2·
H), filter pressure 0.1MPa, backwash pressure 0.15MPa, membrane aperture is 0.02-0.03 μm, using external-compression type film；It is described anti-
When osmosis system processing, water production control flux is 16-18L/ (m2H), using pollution-resistant brackish water desalination film, intake pressure
For 1.2-1.5MPa.
Abrasive waste water variation water quality is larger, passes through the control of above-mentioned process conditions, it is ensured that stable effluent quality.
Processing system and processing method in the present invention are based on the principle that 1, abrasive waste water is through the uniform water quality of conditioning tank
After water, it is pumped into coagulating sedimentation system, by way of dosing coagulating sedimentation, small suspended matter coacervating large particle is made to suspend
Object removes most suspended matters in water and a small amount of COD.Small grind uses dosing coagulating sedimentation in abrasive waste water
Clearly, but SS higher in waste water, PAC, the PAM added is also relatively more for removal effect, and water outlet has certain PAC, PAM
Residual, while the partial size that is milled is very small, has from nanoscale to micron order, be discharged after pretreatment still have a small amount of milling and
PAC,PAM.2, the supernatant after precipitating, which enters in activated sludge+MBR, to be handled, and the respiration of microorganism, flocculation are utilized
Small milling and PAC, PAM are captured and combined, the crown_interception of MBR biomembrane is recycled, removes useless water part COD, residual
Medicament, SS and milling are stayed, water outlet is almost without milling and PAC, PAM, it is ensured that the stable operation of subsequent intermediate water reuse system,
When waste water enters the second reuse water treatment system, the service life of ultrafiltration membrane and reverse osmosis membrane can be greatly improved.
In the present invention, MBR system, which produces water, can reach general reuse requirement, and greening water is directly used in after decontamination system
Deng can be directly discharged to municipal sewage pipe network, that is, enter the first recycle-water processing system when not needing reuse or the when of being further processed
System.If higher to water quality requirement, MBR system produces water and needs after further treatment, i.e., to filter through ultrafiltration system, removes and remains in waste water
Part microorganism, SS etc., ultra-filtration water water quality reaches after counter-infiltration system water inlet requires, then carries out desalination through counter-infiltration system
Processing enters the second reuse water treatment system.
Compared with the prior art, the advantages of the present invention are as follows:
1, the invention firstly uses most of SS etc. in coagulating sedimentation system removal waste water, activated sludge system is recycled
System, the small milling of the MBR system retention overwhelming majority and PAM, PAC, MBR system water outlet pass through at the second reuse water collection system
It when reason, solves the problems, such as ultrafiltration membrane blocking, and MBR film easy cleaning, carries out chemical cleaning when reaching certain negative pressure.It solves
The problem of general Treated sewage reusing technique ultrafiltration membrane blocking, film are run membrane lifetime 3 years or more, are better than general treatment process 1-2
Year.
2, abrasive waste water variation water quality is larger, and materializing strategy phase process effect is unstable, using glass cover of the invention
The processing system of plate abrasive waste water has stable effluent quality, and impact resistance is strong, strong flexibility.
3, the processing system of the glass cover-plate abrasive waste water in the present invention, by the first reuse water collection system and/or the
Two reuse water collection systems carry out reuse, and RO concentrated water can reach 4 three-level mark of " integrated wastewater discharge standard " (GB8978-1996) table
More than standard, without handling again, it is directly discharged to municipal wastewater processing pipe network.After MBR water outlet is sterile-processed after sterilized, water
Matter meets " urban sewage reutilization industry water standard " (GB/T 19923-2005) and " urban sewage reutilization city
City's miscellaneous water water quality " (GB/T 18920-2002) requirement, used as secondary recycle-water.
4, grey water system reclamation rate of the invention is high, and reuse produces water up to 70% or so of water inlet, and production water can be used for big absolutely
Part of production saves great lot of water resources.
Detailed description of the invention
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below
There is attached drawing needed in technical description to be briefly described, it should be apparent that, the accompanying drawings in the following description is the present invention
Some embodiments for those of ordinary skill in the art without creative efforts, can also basis
These attached drawings obtain other attached drawings.
Fig. 1 is the structural schematic diagram of waste water treatment system of the invention.
Fig. 2 is another structural schematic diagram of waste water treatment system of the invention.
Marginal data:
1, wastewater equalization pond；2, coagulating sedimentation system；21, pH conditioning tank；22, coagulation reaction tank；23, flocculation tank；
24, sedimentation basin；25, pH adjusts back pond；26, PAC feed opening；27, PAM feed opening；3, activated Sludge System；4, MBR system；5,
One reuse water collection system；51, decontamination system；52, the first recycle-water tank；6, the second reuse water collection system；61, ultrafiltration
System；62, counter-infiltration system；63, the second recycle-water tank；7, anoxic pond.
Specific embodiment
To facilitate the understanding of the present invention, the present invention is made below in conjunction with Figure of description and preferred embodiment more complete
Face meticulously describes, but the protection scope of the present invention is not limited to the following specific embodiments.
Unless otherwise defined, all technical terms used hereinafter and the normally understood meaning of those skilled in the art
It is identical.Technical term used herein is intended merely to the purpose of description specific embodiment, is not intended to the limitation present invention
Protection scope.
Unless otherwise specified, various raw material, reagent, the instrument and equipment etc. used in the present invention can pass through city
Field is commercially available or can be prepared by existing method.
Embodiment:
As shown in Figure 1, the processing system of the glass cover-plate abrasive waste water of the present embodiment, the waste water including being sequentially communicated is adjusted
Pond 1, coagulating sedimentation system 2, anoxic pond 7, activated Sludge System 3 and MBR system 4, the water outlet of MBR system 4 pass through connecting line
It is communicated with the first reuse water collection system 5 and/or the second reuse water collection system 6；First reuse water collection system 5 includes disinfection
System 51 and the first recycle-water tank 52；Second reuse water collection system 6 includes the ultrafiltration system 61, reverse osmosis being sequentially communicated
System 62 and the second recycle-water tank 63.
In the present embodiment, coagulating sedimentation system 2 includes the pH conditioning tank 21 being sequentially communicated, coagulation reaction tank 22, flocculates instead
Pond 23, sedimentation basin 24 and pH readjustment pond 25, coagulation reaction tank 22 is answered to be equipped with PAC feed opening 26, flocculation tank 23 is equipped with
PAM feed opening 27.
In the present embodiment, the sludge reflux that MBR system 4 is discharged is to anoxic pond 7.
The processing method of the glass cover-plate abrasive waste water of the present embodiment, comprising the following steps:
S1: it sinks coagulation is pumped into again after the water quality and quantity of the glass cover-plate abrasive waste water injection adjusting waste water of wastewater equalization pond 1
Acid/base is added in pH conditioning tank 21 in shallow lake system 2, controls the pH of waste water in 8-9, PAC is added in coagulation reaction tank 22, wadding
PAM is added in solidifying reaction tank 23, makes small suspended matter coacervating large particle suspended matter, carries out muddy water point in sedimentation basin 24 later
From acid adjustment pH to 7 or so is added in supernatant to pH readjustment pond 25, collects supernatant.
S2: supernatant is denitrogenated by anoxic pond 7 by denitrifying bacteria；It is handled using activated Sludge System 3,
Using the suction-operated of aerobic activated sludge, PAM, the PAC and tiny glass not precipitated completely in waste water by coagulating are adsorbed
Glass milling, while removing part COD；Waste water finally passes through MBR system 4, by the filtration of MBR film, containing PAM, PAC with
And the activated sludge of milling is trapped in outside film wire, waste water produces water collecting pit by film wire inner passage to MBR；Containing PAM,
The activated sludge partial discharge of PAC and milling, it is ensured that the content of activated sludge in pond collects the water outlet of MBR system 4.
S3: being delivered to the first reuse water collection system 5 and/or the second reuse water collection system 6 for the water outlet of MBR system 4,
When being delivered to the first reuse water collection system 5, the water outlet of MBR system 4 flows into the first recycle-water water storage after decontamination system 51
Pond 52；When being delivered to the second reuse water collection system 6, ultrafiltration system 61, counter-infiltration system are successively passed through in the water outlet of MBR system 4
The second recycle-water tank 63 is flowed into after 62；When being delivered to the first reuse water collection system 5 and the second reuse water collection system 6,
The water outlet of MBR system 4 is divided into two-way and inputs the first reuse water collection system 5 and the second reuse water collection system 6, after treatment
Respectively reach the first recycle-water tank 52 and the second recycle-water tank 63.
In the present embodiment, as shown in Fig. 2, anoxic pond 7 can also be omitted.
Application Example 1:
Glass cover-plate abrasive waste water is handled using processing system shown in Fig. 2 in the present embodiment, glass cover-plate grinding is useless
Bulky one phase of the pears waste water (its parameter see the table below 1) of Shui Lan Cisco skill, the water outlet of MBR system 4 pass through the first recycle-water respectively and collect system
System 5 and second reuse water collection system 6 handle, detailed process the following steps are included:
S1: it sinks coagulation is pumped into again after the water quality and quantity of the glass cover-plate abrasive waste water injection adjusting waste water of wastewater equalization pond 1
Shallow lake system 2, reaction time of the waste water in pH conditioning tank 21 are 10min, and the pH value that acid/base control waste water is added is 8-9；It is useless
Reaction time of the water in coagulation reaction tank 22 is 30min, and the PAC processing of 150mg/L is added；Waste water is in flocculation tank 23
In reaction time be 30min, and be added 1.5mg/L PAM processing；Sedimentation time of the waste water in sedimentation basin 24 is not less than
2h, surface loading are controlled in 0.8m3/(m2H) below；Reaction time of the waste water in pH readjustment pond 25 is 20min, and is added
The pH value of acid control waste water is 7 or so.
S2: supernatant is handled by activated Sludge System 3, controls residence time of the waste water in activated Sludge System 3
8h, controls DO content 3.5mg/L in activated Sludge System 3, and activated sludge content is 3000mg/L；Waste water finally passes through MBR system
System 4, controlling residence time of the waste water in MBR system 4 is 2h, and permeant flux is in 15L/ (m2H), going out for MBR system 4 is collected
Water.
S3: being delivered to the first reuse water collection system 5 or the second reuse water collection system 6 for the water outlet of MBR system 4, defeated
When sending to the first reuse water collection system 5, the water outlet of MBR system 4 flows into the first recycle-water tank after decontamination system 51
52；When being delivered to the second reuse water collection system 6, ultrafiltration system 61, counter-infiltration system 62 are successively passed through in the water outlet of MBR system 4
After flow into the second recycle-water tank 63.When the processing of ultrafiltration system 61, water production control flux is 50L/ (m2H), filter pressure
For 0.1MPa, backwash pressure 0.15MPa, membrane aperture is 0.02 μm, using external-compression type film；When the processing of counter-infiltration system 62, control
Permeant flux processed is 16L/ (m2H), using pollution-resistant brackish water desalination film, intake pressure 1.2MPa.
After treatment, property is as shown in table 1 below for waste water in the present embodiment.
Reuse aqueous nature after bulky one phase of the pears waste water of 1: Lan Sike skill of table and processing
| Project | COD(mg/L) | SS(mg/L) | Ammonia nitrogen (mg/L) | Conductivity (μ S/cm) |
| Water inlet | 200-300 | 2000-3000 | 10-20 | 600-800 |
| Secondary recycle-water | 30-50 | ≤5 | 2-5 | ≤800 |
| Recycle-water | ≤10 | ND | ≤0.5 | ≤50 |
In upper table, secondary recycle-water is obtained after the processing of the first reuse water collection system 5, and recycle-water passes through second
It is obtained after the processing of reuse water collection system 6.
Application Example 2:
Glass cover-plate abrasive waste water is handled using processing system shown in FIG. 1 in the present embodiment, glass cover-plate grinding is useless
The bulky pears second phase waste water of Shui Lan Cisco skill (its parameter see the table below 2), the water outlet of MBR system 4 pass through the first recycle-water respectively and collect system
System 5 and second reuse water collection system 6 handle, detailed process the following steps are included:
S1: it sinks coagulation is pumped into again after the water quality and quantity of the glass cover-plate abrasive waste water injection adjusting waste water of wastewater equalization pond 1
Shallow lake system 2, reaction time of the waste water in pH conditioning tank 21 are 20min, and the pH value that acid/base control waste water is added is 8-9；It is useless
Reaction time of the water in coagulation reaction tank 22 is 30min, and the PAC processing of 120mg/L is added；Waste water is in flocculation tank 23
In reaction time be 30min, and be added 1.8mg/L PAM processing；Sedimentation time of the waste water in sedimentation basin 24 is not less than
2h, surface loading are controlled in 0.8m3/(m2H) below；Reaction time of the waste water in pH readjustment pond 25 is 20min, and is added
The pH value of acid control waste water is 7 or so.
S2: supernatant is denitrogenated by anoxic pond 7 by denitrifying bacteria；It is handled using activated Sludge System 3,
Residence time 6h of the waste water in activated Sludge System 3 is controlled, DO content 3.0mg/L in activated Sludge System 3 is controlled, activity is dirty
Cement content is 3000mg/L；Waste water finally passes through MBR system 4, and controlling residence time of the waste water in MBR system 4 is 2h, produces water
Flux is in 13L/ (m2H), the water outlet of MBR system 4 is collected.
S3: being delivered to the first reuse water collection system 5 or the second reuse water collection system 6 for the water outlet of MBR system 4, defeated
When sending to the first reuse water collection system 5, the water outlet of MBR system 4 flows into the first recycle-water tank after decontamination system 51
52；When being delivered to the second reuse water collection system 6, ultrafiltration system 61, counter-infiltration system 62 are successively passed through in the water outlet of MBR system 4
After flow into the second recycle-water tank 63.When the processing of ultrafiltration system 61, water production control flux is 45L/ (m2H), filter pressure
For 0.1MPa, backwash pressure 0.15MPa, membrane aperture is 0.03 μm, using external-compression type film；When the processing of counter-infiltration system 62, control
Permeant flux processed is 17L/ (m2H), using pollution-resistant brackish water desalination film, intake pressure 1.4MPa.
After treatment, property is as shown in table 2 below for waste water in the present embodiment.
Reuse aqueous nature after the bulky pears second phase waste water of 2: Lan Sike skill of table and processing
| Project | COD(mg/L) | SS(mg/L) | Ammonia nitrogen (mg/L) | Conductivity (μ S/cm) |
| Water inlet | 200-300 | 2000-3000 | 10-20 | 600-800 |
| Secondary recycle-water | 30-50 | ≤5 | 2-5 | ≤800 |
| Recycle-water | ≤10 | ND | ≤0.5 | ≤50 |
Application Example 3:
This application embodiment is compared with Application Example 1, the difference is that wastewater source is different, in this application embodiment
For wastewater source in blue Cisco's skill Liuyang Nan Yuanyi phase waste water, property is as shown in table 3 below.
After treatment, property is as shown in table 3 below for waste water in the present embodiment.
Reuse aqueous nature after 3: Lan Sike skill Liuyang Nan Yuanyi phase of table waste water and processing
| Project | COD(mg/L) | SS(mg/L) | Ammonia nitrogen (mg/L) | Conductivity (μ S/cm) |
| Water inlet | 200-300 | 2000-5000 | 10-20 | 800-1000 |
| Secondary recycle-water | 30-50 | ≤5 | 2-5 | ≤1000 |
| Recycle-water | ≤10 | ND | ≤0.5 | ≤50 |
Claims (10)
1. a kind of processing system of glass cover-plate abrasive waste water, which is characterized in that including be sequentially communicated wastewater equalization pond (1),
The water outlet of coagulating sedimentation system (2), activated Sludge System (3) and MBR system (4), the MBR system (4) passes through connecting line
It is communicated with the first reuse water collection system (5) and/or the second reuse water collection system (6)；
The first reuse water collection system (5) includes decontamination system (51) and the first recycle-water tank (52)；
The second reuse water collection system (6) includes the ultrafiltration system (61) being sequentially communicated, counter-infiltration system (62) and second
Recycle-water tank (63).
2. the processing system of glass cover-plate abrasive waste water according to claim 1, which is characterized in that the coagulating sedimentation system
It (2) include that the pH conditioning tank (21) being sequentially communicated, coagulation reaction tank (22), flocculation tank (23), sedimentation basin (24) and pH are returned
It adjusts pond (25).
3. the processing system of glass cover-plate abrasive waste water according to claim 2, which is characterized in that the coagulation reaction tank
(22) PAC feed opening (26) are equipped with, the flocculation tank (23) is equipped with PAM feed opening (27).
4. the processing system of glass cover-plate abrasive waste water described in any one of -3 according to claim 1, which is characterized in that described mixed
Anoxic pond (7) are additionally provided between solidifying settling system (2) and activated Sludge System (3).
5. the processing system of glass cover-plate abrasive waste water according to claim 4, which is characterized in that MBR system (4) row
Sludge reflux out is to the anoxic pond (7).
6. a kind of processing method of glass cover-plate abrasive waste water, which comprises the following steps:
S1: it is pumped into coagulating sedimentation again after glass cover-plate abrasive waste water injection wastewater equalization pond (1) to be adjusted to the water quality and quantity of waste water
System (2) after dosing coagulating sedimentation, collects supernatant；
S2: by supernatant by anoxic pond (7), activated Sludge System (3) and MBR system (4), going out for MBR system (4) is collected
Water；
S3: the water outlet of MBR system (4) is delivered to the first reuse water collection system (5) and/or the second reuse water collection system
(6), when being delivered to the first reuse water collection system (5), the water outlet of MBR system (4) flows into first after decontamination system (51)
Recycle-water tank (52)；When being delivered to the second reuse water collection system (6), ultrafiltration system is successively passed through in the water outlet of MBR system (4)
System (61), counter-infiltration system (62) flow into the second recycle-water tank (63) afterwards；Be delivered to the first reuse water collection system (5) and
When the second reuse water collection system (6), the water outlet of MBR system (4) is divided into two-way and inputs the first reuse water collection system (5) and the
Two reuse water collection systems (6) respectively reach the first recycle-water tank (52) and the second recycle-water tank after treatment
(63)。
7. the processing method of glass cover-plate abrasive waste water according to claim 6, which is characterized in that the glass cover-plate grinding
Waste water is after wastewater equalization pond (1) adjusts the water quality and quantity of waste water, COD 200-300mg/L, SS 2000-5000mg/
L, ammonia nitrogen 10-20mg/L, conductivity are 600-800 μ s/cm.
8. the processing method of glass cover-plate abrasive waste water described according to claim 6 or 7, which is characterized in that the coagulating sedimentation
System (2) include the pH conditioning tank (21) being sequentially communicated, coagulation reaction tank (22), flocculation tank (23), sedimentation basin (24) and
PH adjusts back pond (25), and reaction time of the waste water in pH conditioning tank (21) is 10-30min, and acid/base control waste water is added
PH value be 8-9；Reaction time of the waste water in coagulation reaction tank (22) is 10-30min, and 100-200mg/L is added
PAC processing；Reaction time of the waste water in flocculation tank (23) is 10-30min, and the PAM of 0.5-2mg/L is added
Processing；Sedimentation time of the waste water in sedimentation basin (24) is not less than 2h, and surface loading is controlled in 0.8m3/(m2H) below；
Reaction time of the waste water in pH readjustment pond (25) is 10-30min, and the pH value that acid control waste water is added is 6.8-7.2.
9. the processing method of glass cover-plate abrasive waste water described according to claim 6 or 7, which is characterized in that the waste water is in work
Property sludge system (3) in residence time 6-10h, DO content 3.0-3.5mg/L in control activated Sludge System (3), activity is dirty
Cement content is 3000mg/L；Residence time of the waste water in MBR system (4) is 2h, and permeant flux is in 12-15L/ (m2·
h)。
10. the processing method of glass cover-plate abrasive waste water described according to claim 6 or 7, which is characterized in that the ultrafiltration system
(61) when handling, water production control flux is 40-50L/ (m2H), filter pressure 0.1MPa, backwash pressure 0.15MPa, film
Aperture is 0.02-0.03 μm, using external-compression type film；When the counter-infiltration system (62) is handled, water production control flux is 16-18L/
(m2H), using pollution-resistant brackish water desalination film, intake pressure 1.2-1.5MPa.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910722267.4A CN110498561A (en) | 2019-08-06 | 2019-08-06 | A kind of processing system and processing method of glass cover-plate abrasive waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910722267.4A CN110498561A (en) | 2019-08-06 | 2019-08-06 | A kind of processing system and processing method of glass cover-plate abrasive waste water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110498561A true CN110498561A (en) | 2019-11-26 |
Family
ID=68587886
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910722267.4A Pending CN110498561A (en) | 2019-08-06 | 2019-08-06 | A kind of processing system and processing method of glass cover-plate abrasive waste water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110498561A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115231766A (en) * | 2022-06-06 | 2022-10-25 | 惠州市成泰环保智能科技有限公司 | Low-emission recycling system for PCB (printed circuit board) production water |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN205635287U (en) * | 2016-05-24 | 2016-10-12 | 厦门理工学院 | MBR sewage treatment system based on PLC |
| CN208594168U (en) * | 2018-05-14 | 2019-03-12 | 广州迪奕科环保科技有限公司 | Precision glass waste water treatment system |
| CN210796110U (en) * | 2019-08-06 | 2020-06-19 | 深圳粤鹏环保技术股份有限公司 | Glass apron grinds processing system of waste water |
-
2019
- 2019-08-06 CN CN201910722267.4A patent/CN110498561A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN205635287U (en) * | 2016-05-24 | 2016-10-12 | 厦门理工学院 | MBR sewage treatment system based on PLC |
| CN208594168U (en) * | 2018-05-14 | 2019-03-12 | 广州迪奕科环保科技有限公司 | Precision glass waste water treatment system |
| CN210796110U (en) * | 2019-08-06 | 2020-06-19 | 深圳粤鹏环保技术股份有限公司 | Glass apron grinds processing system of waste water |
Non-Patent Citations (1)
| Title |
|---|
| 穆美强等: "TFT 玻璃研磨废水回收再利用系统设计", 《科技视界》 * |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115231766A (en) * | 2022-06-06 | 2022-10-25 | 惠州市成泰环保智能科技有限公司 | Low-emission recycling system for PCB (printed circuit board) production water |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US8999170B2 (en) | Peak flow management in wastewater treatment using direct membrane filtration | |
| CN101544448B (en) | Method for reusing municipal wastewater for circulating-cooling water and power-plant boiler feedwater | |
| CN105859055B (en) | An integrated technology for quality separation and reuse of complex printing and dyeing wastewater | |
| CN101074141B (en) | Low-concentration organic wastewater regeneration and reuse process | |
| CN103351088B (en) | Treatment and regenerative cyclic utilization device for tobacco sheet production wastewater | |
| CN103626352A (en) | Advanced treatment and recycling process and apparatus for sewage reaching standard | |
| CN109264939A (en) | The processing method and system of Lithium Battery Industry production waste water | |
| CN109455849A (en) | Bi-membrane method recycled water advanced treatment based on control membrane fouling improves technique and device | |
| CN107055933A (en) | A kind of high ammonia nitrogen low carbon/nitrogen ratio domestic sewage processing system and method | |
| CN1970474A (en) | Garbage leachate processing process and system based on membrane bioreactor-nano filtering membrane technology | |
| CN109293145A (en) | The method that textile waste is back to Thermal Power Generation Industry | |
| CN101723551B (en) | Coking wastewater recycling treatment method | |
| CN113149352A (en) | System and method for deeply recycling urban reclaimed water into industrial water of thermal power plant | |
| CN106587538A (en) | Method for treating excrement and urine wastes | |
| CN104445835A (en) | Garbage leachate treatment method and system applicable to small towns | |
| CN208327721U (en) | A kind of processing unit of landfill leachate | |
| CN110498561A (en) | A kind of processing system and processing method of glass cover-plate abrasive waste water | |
| CN201648189U (en) | Separating and combining device for regenerating and reclaiming film of electronic industrial wastewater | |
| CN210796110U (en) | Glass apron grinds processing system of waste water | |
| CN220432544U (en) | Papermaking industry waste water recovery system | |
| CN209974485U (en) | Wastewater treatment system | |
| CN208617634U (en) | A kind of leachate in garbage transfer station processing system | |
| CN201317719Y (en) | Integrative combined device for regeneration of papermaking wastewater | |
| CN108675548B (en) | Domestic sewage treatment process and treatment system | |
| CN218371997U (en) | Ultraviolet-positive impact coupling water treatment device |
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 | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20191126 |
|
| RJ01 | Rejection of invention patent application after publication |