CN110156258A - A kind of advanced sewage treatment system and technique - Google Patents
A kind of advanced sewage treatment system and technique Download PDFInfo
- Publication number
- CN110156258A CN110156258A CN201910423988.5A CN201910423988A CN110156258A CN 110156258 A CN110156258 A CN 110156258A CN 201910423988 A CN201910423988 A CN 201910423988A CN 110156258 A CN110156258 A CN 110156258A
- Authority
- CN
- China
- Prior art keywords
- activated coke
- bed filter
- filtrate
- fiber
- haydite
- 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
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—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
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/08—Chemical Oxygen Demand [COD]; Biological Oxygen Demand [BOD]
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/10—Solids, e.g. total solids [TS], total suspended solids [TSS] or volatile solids [VS]
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/14—NH3-N
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/16—Total nitrogen (tkN-N)
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/18—PO4-P
-
- 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
- C02F3/28—Anaerobic digestion processes
- C02F3/2806—Anaerobic processes using solid supports for microorganisms
Abstract
The present invention discloses a kind of advanced sewage treatment system, including sequentially connected flotation tank, denitrification deep-bed filter, activated coke absorption tower, and flotation tank is equipped with PAC adding of agent mouth and PAM adding of agent mouth, for chemistry except total phosphorus and removal SS；The filtrate of denitrification deep-bed filter is using quartz sand, haydite and fiber-like wastes of crops mixing composition, for removing total nitrogen；The filtrate on activated coke absorption tower is activated coke and zeolite mixing composition, for removing COD and ammonia nitrogen.Invention additionally discloses a kind of sewerage advanced treatment process.The present invention is combined using flotation tank, denitrification deep-bed filter, activated coke absorption tower, can be removed COD, ammonia nitrogen, total nitrogen, total phosphorus and the SS in sewage simultaneously, be can guarantee the qualified discharge of each index of tail water, simple, effective, stable.
Description
Technical field
The present invention relates to technical field of sewage, and in particular to a kind of advanced sewage treatment system and technique.
Background technique
In the further treatment technique of sewage, denitrification deep-bed filter is one of main technology, but due to sewage plant two
Grade is discharged carbon source needed for remaining carbon source is insufficient for denitrification biological denitrogenation, it usually needs carbon source is additionally added, so with
Conventional denitrification carbon source is replaced rich in a large amount of fiber-like wastes of crops, moreover it is possible to be provided with the table for adhering to conducive to microorganism and surviving
Area, but pure fiber-like wastes of crops have the characteristics that as the filtrate of denitrification deep-bed filter it is easy to wear.
In addition, advanced treatment of wastewater should develop to simple, effective, stabilising direction.
Summary of the invention
It is an object of the present invention to provide a kind of advanced sewage treatment system and techniques, so as to solve the deficiencies in the prior art.
The invention adopts the following technical scheme:
A kind of advanced sewage treatment system, including sequentially connected flotation tank, denitrification deep-bed filter, activated coke absorb
Tower, flotation tank are equipped with PAC adding of agent mouth and PAM adding of agent mouth, for chemistry except total phosphorus and removal SS；The filter of denitrification depth bed
The filtrate in pond is using quartz sand, haydite and fiber-like wastes of crops mixing composition, for removing total nitrogen；Activated coke absorption tower
Filtrate is activated coke and zeolite mixing composition, for removing COD and ammonia nitrogen.
Further, the filtrate of denitrification deep-bed filter by quartz sand, haydite and fiber-like wastes of crops by volume
3:2:1 mixing composition.
Further, quartz sand particle size 2-4mm；Haydite partial size is 4-8mm；Fiber-like wastes of crops include stalk,
Rice husk, sawdust, bagasse, corncob.
Further, the filtrate on property coke absorption tower is made of activated coke and zeolite 4-2:1 mixing by volume.
Further, activated coke is that coal quality seed activity is burnt, and partial size 2-8mm, iodine number is greater than 600mg/g；Sized zeolite particles
For 2-4mm.
A kind of sewerage advanced treatment process, includes the following steps:
Step 1: sewage is handled through biochemistry pool, water outlet COD is not higher than 80mg/L, and ammonia nitrogen is not higher than 15mg/L, and total phosphorus is not high
It is not higher than 20mg/L in 1.5mg/L, SS, total nitrogen is not higher than 20mg/L, introduces flotation tank afterwards, PAC solution and PAM solution is added,
For chemistry except total phosphorus and removal SS, flotation tank is discharged SS control in 5mg/L；
Step 2: flotation tank water outlet introduces denitrification deep-bed filter, quartz sand, haydite and fiber-like wastes of crops are utilized
The microorganism grown on the filtrate of composition is mixed, in the environment of anoxic, denitrification is carried out, thus total in sewage of degrading
Nitrogen, denitrification deep-bed filter water outlet total nitrogen reach 1.5mg/L or less；
Step 3: the water outlet of denitrification deep-bed filter introduces activated coke absorption tower, formed using active carbon and zeolite mixing
Filtrate passes through physisorption and removes COD and ammonia nitrogen in sewage simultaneously, denitrification deep-bed filter be discharged COD20mg/L with
Under, ammonia nitrogen 1mg/L or less.
Further, 3:2:1 is mixed by volume for quartz sand, haydite and fiber-like wastes of crops.
Further, quartz sand particle size 2-4mm；Haydite partial size is 4-8mm；Fiber-like wastes of crops include stalk,
Rice husk, sawdust, bagasse, corncob.
Further, 4-2:1 is mixed by volume for activated coke and zeolite.
Further, activated coke is that coal quality seed activity is burnt, and partial size 2-8mm, iodine number is greater than 600mg/g；Sized zeolite particles
For 2-4mm.
Beneficial effects of the present invention:
1, the present invention is combined using flotation tank, denitrification deep-bed filter, activated coke absorption tower, can be removed in sewage simultaneously
COD, ammonia nitrogen, total nitrogen, total phosphorus and SS, can guarantee the qualified discharge of each index of tail water, it is simple, effectively, stablize.
2, the present invention is in denitrification deep-bed filter, for the defect for overcoming fiber-like wastes of crops itself, in conjunction with tradition
Quartz sand filter media, the preferable haydite of reselection porosity select quartz sand, haydite and fiber-like wastes of crops body as filtrate
Proportion of the product than 3:2:1 realizes the economic stability operation of denitrification deep-bed filter.Quartz sand and haydite, which combine, increases the strong of filtrate
Degree and porosity (porosity increases, that is, increases the bond area of removal total nitrogen microorganism), fiber-like wastes of crops increases hole
While gap rate, carbon source needed for emphasis provides denitrification.Traditional filtrate quartz sand, haydite and fiber-like wastes of crops
Combination the shortcomings that can overcoming traditional filtrate addition carbon source, while the disadvantage for overcoming fiber-like wastes of crops intensity inadequate,
It ensure that outlet effect, and saved cost.
3, activated coke adsorption tower of the present invention is set to after denitrification deep-bed filter, is conducive to absorb fine in denitrification process
The COD that class wastes of crops generates is tieed up, while being adsorbed the COD in sewage by filtering suction-operated, and activated coke pair
The removal effect of ammonia nitrogen is smaller, carries out Adsorption to ammonia nitrogen by zeolite, it can keep two indexes up to standard, improve the association of the two
Same filtration.Using activated coke and zeolite, 4-2:1 is mixed by volume, can remove tail water and the leaching of fiber-like wastes of crops
COD and ammonia nitrogen out guarantee each index emission compliance in tail water.
Detailed description of the invention
Fig. 1 is present system schematic diagram.
Specific embodiment
The present invention is done below with reference to embodiment and attached drawing and is further explained.The following example is merely to illustrate this hair
It is bright, but be not used to limit practical range of the invention.
A kind of advanced sewage treatment system, as shown in Figure 1, including sequentially connected flotation tank, denitrification deep-bed filter, work
Property coke absorption tower.
Flotation tank is equipped with PAC adding of agent mouth and PAM adding of agent mouth, for chemistry except total phosphorus and removal SS.
3:2:1 is mixed by volume using quartz sand, haydite and fiber-like wastes of crops for the filtrate of denitrification deep-bed filter
It is combined into, quartz sand particle size 2-4mm；Haydite partial size is 4-8mm；Fiber-like wastes of crops include stalk, rice husk, sawdust,
Bagasse, corncob.Denitrification deep-bed filter is for removing total nitrogen.
The filtrate on activated coke absorption tower is activated coke and the zeolite composition of 4-2:1 mixing by volume, and activated coke is coal quality
Grain activated coke, partial size 2-8mm, iodine number are greater than 600mg/g；Sized zeolite particles are 2-4mm.Activated coke absorption tower is for removing COD
And ammonia nitrogen.
A kind of sewerage advanced treatment process, includes the following steps:
Step 1: sewage is handled through biochemistry pool, water outlet COD is not higher than 80mg/L, and ammonia nitrogen is not higher than 15mg/L, and total phosphorus is not high
In 1.5mg/L, SS is not higher than 20mg/L, and total nitrogen is not higher than 20mg/L, introduces flotation tank afterwards, be added 3-10wt%PAC solution and
‰ PAM solution of 0.5-2wt, additive amount are 1-5ml/L sewage, and except total phosphorus and removal SS, flotation tank is discharged SS control and exists chemistry
5mg/L。
Step 2: flotation tank water outlet introduces denitrification deep-bed filter, quartz sand, haydite and fiber-like wastes of crops are utilized
The microorganism grown on the filtrate of the composition of 3:2:1 mixing by volume carries out denitrification in the environment of anoxic, thus
Total nitrogen in degradation sewage, denitrification deep-bed filter water outlet total nitrogen reach 1.5mg/L or less；Wherein, quartz sand particle size 2-
4mm；Haydite partial size is 4-8mm；Fiber-like wastes of crops includes stalk, rice husk, sawdust, bagasse, corncob.
Step 3: the water outlet of denitrification deep-bed filter introduces activated coke absorption tower, active carbon and zeolite 4- by volume are utilized
The filtrate of 2:1 mixing composition, COD and ammonia nitrogen in sewage are removed by physisorption simultaneously, and denitrification deep-bed filter goes out
Water COD20mg/L is hereinafter, ammonia nitrogen 1mg/L or less；Wherein, activated coke is that coal quality seed activity is burnt, partial size 2-8mm, and iodine number is big
In 600mg/g；Sized zeolite particles are 2-4mm.
Claims (10)
1. a kind of advanced sewage treatment system, which is characterized in that including sequentially connected flotation tank, denitrification deep-bed filter, work
Property coke absorption tower, flotation tank be equipped with PAC adding of agent mouth and PAM adding of agent mouth, for chemistry except total phosphorus and removal SS；Anti- nitre
Change the filtrate of deep-bed filter using quartz sand, haydite and fiber-like wastes of crops mixing composition, for removing total nitrogen；Activated coke
The filtrate on absorption tower is activated coke and zeolite mixing composition, for removing COD and ammonia nitrogen.
2. advanced sewage treatment system according to claim 1, which is characterized in that the filtrate of denitrification deep-bed filter is by stone
Sand, haydite and fiber-like the wastes of crops composition of 3:2:1 mixing by volume.
3. advanced sewage treatment system according to claim 1, which is characterized in that quartz sand particle size 2-4mm；Haydite grain
Diameter is 4-8mm；Fiber-like wastes of crops includes stalk, rice husk, sawdust, bagasse, corncob.
4. advanced sewage treatment system according to claim 1, which is characterized in that the filtrate on property coke absorption tower is by activated coke
With the zeolite composition of 4-2:1 mixing by volume.
5. advanced sewage treatment system according to claim 1, which is characterized in that activated coke is that coal quality seed activity is burnt,
Partial size is 2-8mm, and iodine number is greater than 600mg/g；Sized zeolite particles are 2-4mm.
6. a kind of sewerage advanced treatment process, which comprises the steps of:
Step 1: sewage is handled through biochemistry pool, water outlet COD is not higher than 80mg/L, and ammonia nitrogen is not higher than 15mg/L, and total phosphorus is not higher than
1.5mg/L, SS are not higher than 20mg/L, and total nitrogen is not higher than 20mg/L, introduces flotation tank afterwards, and PAC solution and PAM solution is added, and change
It learns except total phosphorus and removal SS, flotation tank is discharged SS control in 5mg/L；
Step 2: flotation tank water outlet introduces denitrification deep-bed filter, mixed using quartz sand, haydite and fiber-like wastes of crops
The microorganism grown on the filtrate of composition carries out denitrification in the environment of anoxic, thus the total nitrogen in sewage of degrading,
Denitrification deep-bed filter water outlet total nitrogen reaches 1.5mg/L or less；
Step 3: the water outlet of denitrification deep-bed filter introduces activated coke absorption tower, the filtrate formed using active carbon and zeolite mixing,
Remove the COD and ammonia nitrogen in sewage simultaneously by physisorption, denitrification deep-bed filter is discharged COD20mg/L hereinafter, ammonia
Nitrogen 1mg/L or less.
7. sewerage advanced treatment process according to claim 6, which is characterized in that quartz sand, haydite and fiber-like farming
3:2:1 is mixed object waste material by volume.
8. sewerage advanced treatment process according to claim 6, which is characterized in that quartz sand particle size 2-4mm；Haydite grain
Diameter is 4-8mm；Fiber-like wastes of crops includes stalk, rice husk, sawdust, bagasse, corncob.
9. sewerage advanced treatment process according to claim 6, which is characterized in that activated coke and zeolite 4-2 by volume:
1 mixing.
10. sewerage advanced treatment process according to claim 6, which is characterized in that activated coke is that coal quality seed activity is burnt,
Partial size is 2-8mm, and iodine number is greater than 600mg/g；Sized zeolite particles are 2-4mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910423988.5A CN110156258A (en) | 2019-05-21 | 2019-05-21 | A kind of advanced sewage treatment system and technique |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910423988.5A CN110156258A (en) | 2019-05-21 | 2019-05-21 | A kind of advanced sewage treatment system and technique |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110156258A true CN110156258A (en) | 2019-08-23 |
Family
ID=67631692
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910423988.5A Pending CN110156258A (en) | 2019-05-21 | 2019-05-21 | A kind of advanced sewage treatment system and technique |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110156258A (en) |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08294699A (en) * | 1995-04-26 | 1996-11-12 | Ebara Corp | Biological denitrification apparatus of waste water |
| CN102092900A (en) * | 2010-12-29 | 2011-06-15 | 江南大学 | Method for treating micro polluted water by using biological nitrogen removal and physicochemical enhanced phosphorus removal combined process |
| CN102249478A (en) * | 2011-05-10 | 2011-11-23 | 襄樊赛洁环保科技有限公司 | Deep nitrogen and phosphorus removal process for surface water body |
| CN105366802A (en) * | 2015-12-11 | 2016-03-02 | 南京大学 | Eco-biofilter apparatus and method for treating sewage by eco-biofilter apparatus |
| CN108862929A (en) * | 2018-08-04 | 2018-11-23 | 浙江水美环保工程有限公司 | The processing system and its processing method of mark transformation are proposed for sewage treatment plant tail water |
| CN109650652A (en) * | 2018-12-24 | 2019-04-19 | 浙江中昌水处理科技有限公司 | Biochemistry pool MBBR technique coupling denitrification deep-bed filter denitrification dephosphorization system and method |
-
2019
- 2019-05-21 CN CN201910423988.5A patent/CN110156258A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08294699A (en) * | 1995-04-26 | 1996-11-12 | Ebara Corp | Biological denitrification apparatus of waste water |
| CN102092900A (en) * | 2010-12-29 | 2011-06-15 | 江南大学 | Method for treating micro polluted water by using biological nitrogen removal and physicochemical enhanced phosphorus removal combined process |
| CN102249478A (en) * | 2011-05-10 | 2011-11-23 | 襄樊赛洁环保科技有限公司 | Deep nitrogen and phosphorus removal process for surface water body |
| CN105366802A (en) * | 2015-12-11 | 2016-03-02 | 南京大学 | Eco-biofilter apparatus and method for treating sewage by eco-biofilter apparatus |
| CN108862929A (en) * | 2018-08-04 | 2018-11-23 | 浙江水美环保工程有限公司 | The processing system and its processing method of mark transformation are proposed for sewage treatment plant tail water |
| CN109650652A (en) * | 2018-12-24 | 2019-04-19 | 浙江中昌水处理科技有限公司 | Biochemistry pool MBBR technique coupling denitrification deep-bed filter denitrification dephosphorization system and method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204848595U (en) | Effluent disposal system breeds | |
| CN102775029A (en) | Advanced municipal wastewater treatment system and method | |
| CN110156242B (en) | Method for efficiently treating aquaculture sewage through cooperation of bacteria and algae | |
| CN111807453A (en) | Modified biochar for adsorbing phosphorus in water body and preparation method and application thereof | |
| CN212770335U (en) | Ecological management system of tail water breeds | |
| JP2017154064A (en) | Method for producing biological active carbon stuck with nitrifying bacteria | |
| CN105585216B (en) | Micro polluted source method for processing water supply depth | |
| CN104098173A (en) | Biological aerated filter provided with suspended bed | |
| CN111056700A (en) | Novel composite wetland system for repairing micro-polluted water body | |
| CN1935683A (en) | Slag treating agent and its process and equipment for treating sewage | |
| CN109912136A (en) | A method of utilizing adsorption treatment ammonia nitrogen waste water culture microalgae | |
| JP2015093257A (en) | Method for regenerating vegetable spherical active carbon and method for reutilizing in water treatment of regenerated vegetable spherical active carbon | |
| CN105621786A (en) | Upwelling vertical constructed wetland system for treating agricultural non-point source pollution | |
| CN210193519U (en) | Adjustable artificial wetland system | |
| CN110156258A (en) | A kind of advanced sewage treatment system and technique | |
| CN208594175U (en) | Sewage treatment system for farm | |
| CN106277602A (en) | The Treated sewage reusing processing system of industrial wastewater and method | |
| CN108314179B (en) | Method for removing nitrogen, phosphorus and refractory toxic organic matters in sewage by reinforced activated sludge | |
| CN106698590B (en) | Resin regeneration anaerobic microbial reactor integrating biological culture and biological reduction and application thereof | |
| CN215102271U (en) | Secondary biochemical effluent ferro-sulphur synergistic polyculture denitrification deep denitrification reactor | |
| CN206266391U (en) | A kind of pre- anticlogging artificial marsh sewage treatment system | |
| CN201825818U (en) | Device for removing organic matter and ammonia nitrogen in aquatic water | |
| CN210103705U (en) | Environment-friendly efficient composite domestic sewage treatment system for thermal power plant | |
| CN108439704A (en) | A kind of river point-source pollution source in-situ treatment system | |
| CN210030315U (en) | Aquaculture sewage treatment equipment |
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 | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20190823 |