CN107235612A - Sewage water treatment method - Google Patents
Sewage water treatment method Download PDFInfo
- Publication number
- CN107235612A CN107235612A CN201710668568.4A CN201710668568A CN107235612A CN 107235612 A CN107235612 A CN 107235612A CN 201710668568 A CN201710668568 A CN 201710668568A CN 107235612 A CN107235612 A CN 107235612A
- Authority
- CN
- China
- Prior art keywords
- sewage
- tank
- parts
- collecting
- treatment method
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- 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
- C02F1/5245—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents using basic salts, e.g. of aluminium and iron
-
- 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
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/16—Nitrogen compounds, e.g. ammonia
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
-
- 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
- C02F3/30—Aerobic and anaerobic 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
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
Abstract
The invention discloses sewage water treatment method, step includes：1) sewage flows into the first collecting-tank after coarse rack；2) aluminium polychloride, polyacrylamide, polyethyleneimine and bentonite are delivered into first collecting-tank；3) sewage of first collecting-tank flows into flocculation tank, flows into sewage sludge processing all-in-one；4) the second collecting-tank is flowed into；5) polyferric chloride, polyacrylamide, polyethyleneimine and bentonite are delivered to the first collecting-tank；5) sewage of second collecting-tank enters anaerobic pond；6) sewage in anaerobic pond enters aerobic aeration pond；7) sewage in Aerobic Pond is flowed into the 3rd collecting-tank；8) sodium chloride, lime, adsorbate, sodium carbonate, iron chloride are put into the 3rd water purifying tank；9) sewage in the 3rd collecting-tank enters filtering ponds.The present invention makes harmful material be converted into harmless material, water to be then purified, and resource is fully utilized, with extensive market application value.
Description
Technical field
The present invention relates to a kind of sewage water treatment method.
Background technology
Water is the source of human life, and existence is originally.With the development of industrial and agricultural production, water environmental problems become more and more tighter
Weight, quality problem has had a strong impact on the normal life of our mankind.Therefore, it is necessary to find effective sewage purification technology with
Realize the sustainable use of water resource.In recent years, people set up many ripe effective sewage water treatment methods, such as domestic big city
The activated sludge process of sewage treatment plant of city.While Activated Sludge Process is applied, AB methods, A/O methods, A2/O methods, CASS methods,
SBR methods, oxidation ditch process, stabilization pond method, land treatment systems method etc. are also applied in the construction of sewage treatment plant.Based on active dirty
The sewage disposal technology advantage of bricklayer's's skill is sewage strong adaptability, and construction cost is relatively low, and has the disadvantage that operation stability is poor, easily
Generation sludge bulking and sludge loss, separating effect are not ideal enough.Activated sludge process mainly uses the biology of microorganism living
Property is made a return journey except the organic matter in sewage, ammonia nitrogen, the pollutant such as phosphorus.It is various different thin in order to reach preferable wastewater treatment efficiency
Flora falls to need to cooperate under different conditions.Such as：Oxidation Decomposition of the heterotrophic bacterium under aerobic condition to organic matter,
Oxidation (nitration reaction) of the autotroph (nitrobacteria) under aerobic condition to ammonia nitrogen, heterotrophic bacterium is under anaerobic
Using organic matter to reduction (anti-nitration reaction) of nitrite/nitrate etc..Generally, it is considered that nitrifying process is in whole ammonia nitrogen
An important process in degradation process, process is slow, and complete difficulty is higher.It is primarily due to nitrobacteria and belongs to autotrophic type
Bacterium, including Nitrosomas and nitric acid Pseudomonas.Two class bacterium are obligate aerobic organism, and final electricity is used as using oxygen in oxidizing process
Sub- acceptor, unique energy source is used as by the use of DIC (being typically carbon dioxide).So the nitrobacteria metabolism time is long, it is raw
Grow very slow, growing environment is harsher, some common nitrous acid strains will averagely take 26 hours and could breed one times, and nitric acid
The cycle of strain reproduction is longer, and averagely to take 60 hours could breed one times.So can not be micro- with heterotroph under the conditions of a lot
Biology gets the mastery in growth competition.Therefore it is often found that in actual sewage treatment plant running, such as A/O techniques are dirty
The nitrification ability of mud gradually weakens with the time limit of operation, is got the mastery mainly due to heterotroph microorganism in growth competition
So that the ratio reduction of nitrobacteria.In view of above-mentioned defect, it would be highly desirable to a kind of sewage water treatment method, make it with more in industry
Value.
The content of the invention
The problem of for being previously mentioned, the invention provides a kind of sewage water treatment method, step includes：
1) treatment sewage is flowed into the first collecting-tank after the intercepted removal partial suspended thing of coarse rack；
2) by weight by 5~10 parts of aluminium polychloride, 8~12 parts of polyacrylamide, 7~10 parts of polyethyleneimine and swollen
7~10 parts of profit soil is delivered into first collecting-tank, stands 10~30min；
3) sewage of first collecting-tank flows into flocculation tank, fully anti-with flocculant in the flocculation tank
Reflect so that partial suspended thing flocculates to be formed after floccule body, inflow sewage sludge processing all-in-one handles one by sewage sludge
After machine, suspension and floccule body are intercepted；
4) sewage after the processing of sewage sludge all-in-one flows into the second collecting-tank；
5) by weight by 20~25 parts of polyferric chloride, 10~14 parts of polyacrylamide, 5~8 parts of polyethyleneimine
Delivered with bentonite to first collecting-tank for 15~20 parts, heat second collecting-tank after standing 40~60min, temperature is
30~50 DEG C, the time is 20~40min；
5) sewage of second collecting-tank enters anaerobic pond, carries out the anti-of nitrate nitrogen with denitrifying bacterium under anoxic conditions
Nitration reaction, removes carbonaceous organic material and itrogenous organic substance in sewage；
6) sewage in anaerobic pond enters aerobic aeration pond, and sewage is contacted with the biologic packing material with aeration flowing, goes decontamination
Organic pollution in water；
7) sewage in Aerobic Pond is flowed into the 3rd collecting-tank；
8) by weight by 10~15 parts of sodium chloride, 0.5~1.5 part of lime, 5~8 parts of adsorbate, 0.5~2 part of sodium carbonate
The 3rd water purifying tank to be put into 5~10 parts of iron chloride, stands and the 3rd collecting-tank is heated after 10~20min, temperature is 30~
50 DEG C, the time is 20~40min；
9) sewage in the 3rd collecting-tank enters filtering ponds, and the filtering ponds are three sections, and first paragraph is filled with
There is water-locator, the second segment is hollow section, the 3rd section or activated carbon section.
Preferred scheme is：The coarse rack, which is intercepted, removes the bulky grain suspension that diameter is more than 8mm.
Preferred scheme is：The scarce filler of denitrifying bacterium is filled with the anaerobic pond.
Preferred scheme is：Filled out in the aerobic aeration pond filled with biology.Material.
Preferred scheme is：The hydraulic detention time in the aerobic aeration pond is 2~4h.
Preferred scheme is：By weight by 5 parts of aluminium polychloride, 8 parts of polyacrylamide, 7 parts of polyethyleneimine and swelling
7 parts of soil is delivered into first collecting-tank, stands 10min.
Preferred scheme is：By weight by 20 parts of polyferric chloride, 10 parts of polyacrylamide, 5 parts of polyethyleneimine and
15 parts of bentonite, which is delivered, arrives second collecting-tank, stands and second collecting-tank is heated after 40min, and temperature is 30 DEG C, time
For 20min.
Preferred scheme is：By weight by 10 parts of sodium chloride；0.5 part of lime；5 parts of adsorbate；0.5 part of sodium carbonate；Chlorination
5 parts of iron puts into the 3rd water purifying tank, stands and the 3rd collecting-tank is heated after 10min, and temperature is 30 DEG C, and the time is 20min.
The present invention uses multistep treatment mode, main to carry out decontamination processing using physics and chemical bonding processes, can be effective
Polluter contained by sewage is separated from the water removal, harmful material is converted into harmless material, water and is then purified,
And resource is fully utilized, with extensive market application value.
Embodiment
The present invention is described in further detail below, to make those skilled in the art being capable of evidence with reference to specification word
To implement.
It should be appreciated that such as " having ", "comprising" and " comprising " term used herein do not allot one or many
The presence or addition of individual other elements or its combination.
Embodiment 1
A kind of sewage water treatment method is present embodiments provided, step includes：
1) treatment sewage is flowed into the first collecting-tank after the intercepted removal partial suspended thing of coarse rack；
2) by weight by 5 parts of aluminium polychloride, 8 parts of polyacrylamide, the 7 parts of dispensings of 7 parts of polyethyleneimine and bentonite
Into first collecting-tank, 10min is stood；
3) sewage of first collecting-tank flows into flocculation tank, fully anti-with flocculant in the flocculation tank
Reflect so that partial suspended thing flocculates to be formed after floccule body, inflow sewage sludge processing all-in-one handles one by sewage sludge
After machine, suspension and floccule body are intercepted；
4) sewage after the processing of sewage sludge all-in-one flows into the second collecting-tank；
5) by weight by 15 parts of 20 parts of polyferric chloride, 10 parts of polyacrylamide, 5 parts of polyethyleneimine and bentonite
Deliver first collecting-tank, stand and second collecting-tank is heated after 40~60min, temperature is 30 DEG C, the time is
20min；
5) sewage of second collecting-tank enters anaerobic pond, carries out the anti-of nitrate nitrogen with denitrifying bacterium under anoxic conditions
Nitration reaction, removes carbonaceous organic material and itrogenous organic substance in sewage；
6) sewage in anaerobic pond enters aerobic aeration pond, and sewage is contacted with the biologic packing material with aeration flowing, goes decontamination
Organic pollution in water；
7) sewage in Aerobic Pond is flowed into the 3rd collecting-tank；
8) by weight by 5 parts of 10~15 parts of sodium chloride, 0.5 part of lime, 5 parts of adsorbate, 0.5 part of sodium carbonate and iron chloride
The 3rd water purifying tank is put into, stands and the 3rd collecting-tank is heated after 10min, temperature is 30 DEG C, and the time is 20min；
9) sewage in the 3rd collecting-tank enters filtering ponds, and the filtering ponds are three sections, and first paragraph is filled with
There is water-locator, the second segment is hollow section, the 3rd section or activated carbon section.
Effluent quality after above-mentioned processing is detected, effluent quality is：Water temperature=12~25 DEG C；COD ＜ 50mg/L,
Clearance more than 90%；BOD5 ＜ 10mg/L, clearance more than 95%；SS ＜ 10mg/L, clearance more than 95%；NH4+-N ＜
5mg/L, clearance more than 95%；TN≤15mg/L, clearance more than 90%；TP≤0.5mg/L, clearance more than 90%；pH
=7.0~8.5.
Embodiment 2
A kind of sewage water treatment method is present embodiments provided, step includes：
1) treatment sewage is flowed into the first collecting-tank after the intercepted removal partial suspended thing of coarse rack；
2) by weight by 10 parts of 10 parts of aluminium polychloride, 12 parts of polyacrylamide, 10 parts of polyethyleneimine and bentonite
Deliver in first collecting-tank, stand 30min；
3) sewage of first collecting-tank flows into flocculation tank, fully anti-with flocculant in the flocculation tank
Reflect so that partial suspended thing flocculates to be formed after floccule body, inflow sewage sludge processing all-in-one handles one by sewage sludge
After machine, suspension and floccule body are intercepted；
4) sewage after the processing of sewage sludge all-in-one flows into the second collecting-tank；
5) by weight by 20 parts of 25 parts of polyferric chloride, 14 parts of polyacrylamide, 8 parts of polyethyleneimine and bentonite
First collecting-tank is delivered, stands and second collecting-tank is heated after 60min, temperature is 50 DEG C, and the time is 40min；
5) sewage of second collecting-tank enters anaerobic pond, carries out the anti-of nitrate nitrogen with denitrifying bacterium under anoxic conditions
Nitration reaction, removes carbonaceous organic material and itrogenous organic substance in sewage；
6) sewage in anaerobic pond enters aerobic aeration pond, and sewage is contacted with the biologic packing material with aeration flowing, goes decontamination
Organic pollution in water；
7) sewage in Aerobic Pond is flowed into the 3rd collecting-tank；
8) by weight by 15 parts of sodium chloride；1.5 parts of lime, 8 parts of adsorbate, 10 parts of inputs of 2 parts of sodium carbonate and iron chloride
To the 3rd water purifying tank, stand and the 3rd collecting-tank is heated after 20min, temperature is 50 DEG C, and the time is 40min；
9) sewage in the 3rd collecting-tank enters filtering ponds, and the filtering ponds are three sections, and first paragraph is filled with
There is water-locator, the second segment is hollow section, the 3rd section or activated carbon section.
Effluent quality after above-mentioned processing is detected, effluent quality is：Water temperature=12~25 DEG C；COD ＜ 45mg/L,
Clearance more than 93%；BOD5 ＜ 8mg/L, clearance more than 97%；SS ＜ 9mg/L, clearance more than 97%；NH4+-N ＜
4mg/L, clearance more than 97%；TN≤13mg/L, clearance more than 95%；TP≤0.3mg/L, clearance more than 94%；pH
=7.0~8.5.
Embodiment 3
A kind of sewage water treatment method is present embodiments provided, step includes：
1) treatment sewage is flowed into the first collecting-tank after the intercepted removal partial suspended thing of coarse rack；
2) by weight by 8 parts of aluminium polychloride, 10 parts of polyacrylamide, the 8 parts of dispensings of 9 parts of polyethyleneimine and bentonite
Into first collecting-tank, 20min is stood；
3) sewage of first collecting-tank flows into flocculation tank, fully anti-with flocculant in the flocculation tank
Reflect so that partial suspended thing flocculates to be formed after floccule body, inflow sewage sludge processing all-in-one handles one by sewage sludge
After machine, suspension and floccule body are intercepted；
4) sewage after the processing of sewage sludge all-in-one flows into the second collecting-tank；
5) by weight by 18 parts of 22 parts of polyferric chloride, 12 parts of polyacrylamide, 7 parts of polyethyleneimine and bentonite
First collecting-tank is delivered, stands and second collecting-tank is heated after 50min, temperature is 40 DEG C, and the time is 30min；
5) sewage of second collecting-tank enters anaerobic pond, carries out the anti-of nitrate nitrogen with denitrifying bacterium under anoxic conditions
Nitration reaction, removes carbonaceous organic material and itrogenous organic substance in sewage；
6) sewage in anaerobic pond enters aerobic aeration pond, and sewage is contacted with the biologic packing material with aeration flowing, goes decontamination
Organic pollution in water；
7) sewage in Aerobic Pond is flowed into the 3rd collecting-tank；
8) by weight by 12 parts of sodium chloride；8 parts of 0.9 part of lime, 7 parts of adsorbate, 1 part of sodium carbonate and iron chloride are put into
3rd water purifying tank, stands and the 3rd collecting-tank is heated after 15min, and temperature is 40 DEG C, and the time is 30min；
9) sewage in the 3rd collecting-tank enters filtering ponds, and the filtering ponds are three sections, and first paragraph is filled with
There is water-locator, the second segment is hollow section, the 3rd section or activated carbon section.
Effluent quality after above-mentioned processing is detected, effluent quality is：Water temperature=12~25 DEG C；COD ＜ 45mg/L,
Clearance more than 94%；BOD5 ＜ 9mg/L, clearance more than 96%；SS ＜ 9.5mg/L, clearance more than 96%；NH4+-N ＜
3.5mg/L, clearance more than 96%；TN≤12mg/L, clearance more than 93%；TP≤0.3mg/L, clearance more than 93%；
PH=7.0~8.5.
Although embodiment of the present invention is disclosed as above, it is not restricted in specification and embodiment listed
With it can be applied to various suitable the field of the invention completely, can be easily for those skilled in the art
Other modification is realized, therefore under the universal limited without departing substantially from claim and equivalency range, the present invention is not limited
In specific details.
Claims (8)
1. sewage water treatment method, it is characterised in that step includes：
1) treatment sewage is flowed into the first collecting-tank after the intercepted removal partial suspended thing of coarse rack；
2) by weight by 5~10 parts of aluminium polychloride, 8~12 parts of polyacrylamide, 7~10 parts of polyethyleneimine and bentonite
7~10 parts are delivered into first collecting-tank, stand 10~30min；
3) sewage of first collecting-tank flows into flocculation tank, fully reflect with flocculant in the flocculation tank with
Make partial suspended thing flocculate to be formed after floccule body, flow into sewage sludge processing all-in-one, after sewage sludge processing all-in-one,
Suspension and floccule body are intercepted；
4) sewage after the processing of sewage sludge all-in-one flows into the second collecting-tank；
5) by weight by 20~25 parts of polyferric chloride, 10~14 parts of polyacrylamide, 5~8 parts of polyethyleneimine and swollen
15~20 parts of profit soil, which is delivered, arrives first collecting-tank, and second collecting-tank is heated after standing 40~60min, and temperature is 30~
50 DEG C, the time is 20~40min；
5) sewage of second collecting-tank enters anaerobic pond, carries out the denitrification of nitrate nitrogen with denitrifying bacterium under anoxic conditions
Reaction, removes carbonaceous organic material and itrogenous organic substance in sewage；
6) sewage in anaerobic pond enters aerobic aeration pond, and sewage is contacted with the biologic packing material with aeration flowing, removed in sewage
Organic pollution；
7) sewage in Aerobic Pond is flowed into the 3rd collecting-tank；
8) by weight by 10~15 parts of sodium chloride, 0.5~1.5 part of lime, 5~8 parts of adsorbate, 0.5~2 part of sodium carbonate and chlorine
Change 5~10 parts of iron and put into the 3rd water purifying tank, stand and the 3rd collecting-tank is heated after 10~20min, temperature is 30~50 DEG C,
Time is 20~40min；
9) sewage in the 3rd collecting-tank enters filtering ponds, and the filtering ponds are three sections, and first paragraph has been filled with cloth
Hydrophone, second segment is hollow section, the 3rd section or activated carbon section.
2. sewage water treatment method according to claim 1, it is characterised in that the coarse rack intercepts removal diameter and is more than
8mm bulky grain suspension.
3. sewage water treatment method according to claim 1, it is characterised in that denitrifying bacterium is filled with the anaerobic pond
Lack filler.
4. sewage water treatment method according to claim 1, it is characterised in that filled with biology in the aerobic aeration pond
Fill out.Material.
5. sewage water treatment method according to claim 1, it is characterised in that the hydraulic detention time in the aerobic aeration pond
For 2~4h.
6. sewage water treatment method according to claim 1, it is characterised in that by weight by 5 parts of aluminium polychloride, poly- third
7 parts of 8 parts of acrylamide, 7 parts of polyethyleneimine and bentonite are delivered into first collecting-tank, stand 10min.
7. sewage water treatment method according to claim 1, it is characterised in that by weight by 20 parts of polyferric chloride,
15 parts of 10 parts of polyacrylamide, 5 parts of polyethyleneimine and bentonite are delivered and arrive second collecting-tank, stand and are heated after 40min
Second collecting-tank, temperature is 30 DEG C, and the time is 20min.
8. sewage water treatment method according to claim 1, it is characterised in that by weight by 10 parts of sodium chloride, lime 0.5
Part, 5 parts of adsorbate, 0.5 part of sodium carbonate and 5 parts of iron chloride put into the 3rd water purifying tank, and the 3rd collection is heated after standing 10min
Pond, temperature is 30 DEG C, and the time is 20min.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710668568.4A CN107235612A (en) | 2017-08-08 | 2017-08-08 | Sewage water treatment method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710668568.4A CN107235612A (en) | 2017-08-08 | 2017-08-08 | Sewage water treatment method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107235612A true CN107235612A (en) | 2017-10-10 |
Family
ID=59989916
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710668568.4A Pending CN107235612A (en) | 2017-08-08 | 2017-08-08 | Sewage water treatment method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107235612A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110668651A (en) * | 2019-10-26 | 2020-01-10 | 马强 | Sewage treatment method for building construction site |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104058559A (en) * | 2014-07-16 | 2014-09-24 | 苏州嘉净环保科技股份有限公司 | Sewage treatment method and sewage treatment system |
-
2017
- 2017-08-08 CN CN201710668568.4A patent/CN107235612A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104058559A (en) * | 2014-07-16 | 2014-09-24 | 苏州嘉净环保科技股份有限公司 | Sewage treatment method and sewage treatment system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110668651A (en) * | 2019-10-26 | 2020-01-10 | 马强 | Sewage treatment method for building construction site |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN108996808B (en) | Biochemical combined treatment process and equipment for degradation-resistant concentrated water in steel industry | |
| Chyan et al. | Improving removal performance of pollutants by artificial aeration and flow rectification in free water surface constructed wetland | |
| JP6445855B2 (en) | Nitrogen treatment method and nitrogen treatment apparatus | |
| Benyoucef et al. | Denitrification of groundwater using Brewer's spent grain as biofilter media | |
| Wu et al. | Response of a tidal operated constructed wetland to sudden organic and ammonium loading changes in treating high strength artificial wastewater | |
| CN102464420B (en) | Sewage physical-chemical treatment method | |
| Zhang et al. | Effects of deoxygenation pretreatment and dissolved oxygen adjustment on performance of double-layer-packed sequencing biofilm batch reactor treating secondary effluent under low temperature | |
| Wu et al. | Microporous intermittent aeration vertical flow constructed wetlands for eutrophic water improvement | |
| Qian et al. | Development and application of some renovated technologies for municipal wastewater treatment in China | |
| CN114291942A (en) | Catalytic electrolysis municipal sewage purification system and purification method | |
| CN107235612A (en) | Sewage water treatment method | |
| KR20190035277A (en) | Sewage treatment system using granule | |
| CN111003816A (en) | Biochemical tail water biological denitrification method for inhibiting non-filamentous bacterium expansion | |
| Rajmohan et al. | Bioremediation of nitrate-contaminated wastewater and soil | |
| Ding et al. | Enhanced Nitrogen Removal of Eutrophic Water in Constructed Wetland by Novel Integration of Submerged Macrophyte Pond. | |
| Song et al. | Performance of a large-scale wetland treatment system in treating tailwater from a sewage treatment plant | |
| Tian et al. | Treatment via the Living Machine system of blackwater collected from septic tanks: effect of different plant groups in the systems | |
| JP3858271B2 (en) | Wastewater treatment method and apparatus | |
| KR100202066B1 (en) | Wastewater treatment method using biological 3 step digestion process in one reactor | |
| CN215403551U (en) | Municipal administration sewage's catalytic electrolysis clean system | |
| Ju et al. | Effect of dissolved oxygen on nitrogen and phosphorus removal rate in Biolak process | |
| Singh et al. | Gray water treatment by water hyacinth—a review | |
| Zhang | Entrapped-mixed-microbial-cell process for removal of carbon and nitrogen in one single reactor | |
| Aalam | Application of constructed wetlands for different wastewater treatment in tropical regions: A review | |
| Miao | Horizontal-flow (HF) constructed wetlands for winery wastewater treatment: A review |
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: 20171010 |
|
| RJ01 | Rejection of invention patent application after publication |