CN107055815A - A kind of osmosis system applied to sewage disposal - Google Patents
A kind of osmosis system applied to sewage disposal Download PDFInfo
- Publication number
- CN107055815A CN107055815A CN201710374365.4A CN201710374365A CN107055815A CN 107055815 A CN107055815 A CN 107055815A CN 201710374365 A CN201710374365 A CN 201710374365A CN 107055815 A CN107055815 A CN 107055815A
- Authority
- CN
- China
- Prior art keywords
- sewage
- room
- dephosphorization
- treatment plant
- ammonia nitrogen
- 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
- 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
- C02F3/348—Biological treatment of water, waste water, or sewage characterised by the microorganisms used characterised by the way or the form in which the microorganisms are added or dosed
-
- 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
- C02F2101/105—Phosphorus 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
Abstract
The invention discloses a kind of osmosis system applied to sewage disposal, including：One sewage-treatment plant, a sewage transport mechanism；The sewage-treatment plant is internally provided with dephosphorization room, ammonia nitrogen removal room and total nitrogen and removes room, and the dephosphorization room, ammonia nitrogen removal room and total nitrogen, which are removed, is filled with sewage disposal filler in room.The turner structure of upset filler is additionally provided with the dephosphorization room.When sewage is flowed into the sewage-treatment plant, phosphorus, ammonia nitrogen and the total nitrogen in sewage can be removed, so as to once remove the multiple element in sewage, is asked the need for meeting user.Simultaneously, by being provided with turner structure in dephosphorization room, the turner structure can constantly overturn filler, and then allow filler preferably with air contact, increase the oxygen content in filler, and then organic matter degradation bacterium in the dephosphorization room and polyP bacteria preferably react with sewage so that the phosphor-removing effect of sewage is more preferable.
Description
Technical field
The present invention relates to sewage treatment area, the infiltration of particularly a kind of phosphorus that can be eliminated in sewage, ammonia nitrogen and total nitrogen
System.
Background technology
It is well known that contain various elements in sewage, damage of the phosphorus, ammonia nitrogen and total nitrogen wherein in sewage to environment
Evil is maximum.
In order to administer sewage, market occurs in that miscellaneous sewage disposal device, but those equipment can only typically be gone
Except certain Partial Elements in sewage, wastewater treatment efficiency is not obvious.
The content of the invention
In order to solve the above problems, it is an object of the invention to provide one kind is simple in construction, while can go in water removal again
Phosphorus, the osmosis system of ammonia nitrogen and total nitrogen.
The present invention is for the technical scheme that uses of its technical problem of solution：
A kind of osmosis system applied to sewage disposal, including：
One sewage-treatment plant,
One sewage transport mechanism；The sewage transport mechanism is used to convey pending sewage to the sewage-treatment plant；
The sewage-treatment plant is internally provided with dephosphorization room, ammonia nitrogen removal room and total nitrogen and removes room, the dephosphorization room, ammonia
Nitrogen removes room and total nitrogen removes and sewage disposal filler is filled with room；
The sewage transport mechanism enters sewage transport in the sewage-treatment plant, and sewage flows successively to be had by described
Dephosphorization room, ammonia nitrogen removal room and total nitrogen remove room；
The turner structure of upset filler is additionally provided with the dephosphorization room, the turner structure includes being movably arranged on institute
State to be provided with the rotary shaft in dephosphorization room, the rotary shaft and multiple turn over throwing oar.
As the improvement of above-mentioned technical proposal, the sewage transport mechanism is arranged above the sewage-treatment plant for one
Sewage conveying tube.
Wherein, sponge iron, manganese sand, organic matter degradation bacterium and polyP bacteria are filled with the dephosphorization room.
Further, it is thin filled with sponge filler, graded broken stone, organic matter degradation bacterium and nitrification in the ammonia nitrogen removal room
Bacterium.
Further, the total nitrogen, which is removed, is filled with pelelith, denitrifying bacteria, corncob and bio-based materials in room.
Herein, it is additionally provided with a filter chamber, the filter chamber and fills out between the ammonia nitrogen removal room and total nitrogen removal room
Filled with rubble.
Further, the dephosphorization room, ammonia nitrogen removal room and filter chamber are cascadingly set on along direction from top to bottom
In the inside of the sewage-treatment plant.
Further, the bottom of the filter chamber is additionally provided with aeration tube.
The beneficial effects of the invention are as follows：Because the present invention in sewage-treatment plant by being internally provided with dephosphorization room, ammonia
Nitrogen removes room and total nitrogen and removes room, when sewage is flowed into the sewage-treatment plant, can remove phosphorus in sewage, ammonia nitrogen and
Total nitrogen, so as to once remove the multiple element in sewage, is asked the need for meeting user；Turned over by being provided with dephosphorization room
Throw mechanism, the turner structure can constantly overturn filler, so allow filler preferably with air contact, increase filler
In oxygen content, and then organic matter degradation bacterium in the dephosphorization room and polyP bacteria preferably react with sewage so that dirty
The phosphor-removing effect of water is more preferable.
The present invention is sprayed into the dirt from the top of sewage-treatment plant again after using atomizer, sewage is atomized simultaneously
In water treatment facilities, in the process, the contact area of sewage and air is increased, and then greatly increase the oxygen-containing of sewage
Amount, in order to which follow-up microorganism is reacted it and eliminates the various elements in sewage；
The present invention in removing room in the dephosphorization room, ammonia nitrogen removal room and total nitrogen filled with sewage disposal by filling out in addition
Material, therefore sewage can only slowly penetrate through dephosphorization room, ammonia nitrogen removal room and total nitrogen removal room successively, sewage is passed through at sewage
Reason device is needed to take longer time, therefore sewage-treatment plant can be more fully handled sewage, and then sewage
Treatment effect is more preferable.
Brief description of the drawings
The present invention is further detailed explanation with reference to the accompanying drawings and detailed description.
Fig. 1 is the structural representation of one embodiment of the present invention.
Embodiment
Reference picture 1, a kind of osmosis system applied to sewage disposal, including a sewage-treatment plant 10 and a sewage transport
Mechanism 20；The sewage transport mechanism 20 is used to convey pending sewage to the sewage-treatment plant 10；The sewage disposal
Device 10 is internally provided with dephosphorization room 11, ammonia nitrogen removal room 12 and total nitrogen and removes room 13, the dephosphorization room 11, ammonia nitrogen removal room 12
And total nitrogen removes and sewage disposal filler is filled with room 13；The sewage transport mechanism 20 enters sewage transport at the sewage
Manage in device 10, sewage flows successively has dephosphorization room 11, ammonia nitrogen removal room 12 and total nitrogen to remove room 13 by described.In this hair
Bright, two adjacent rooms are interconnected in the sewage-treatment plant 10, i.e., described dephosphorization room 11 is connected with ammonia nitrogen removal room 12
It is logical, and ammonia nitrogen removal room 12 then removes room 13 with total nitrogen and is connected.
Because the present invention in sewage-treatment plant 10 by being internally provided with dephosphorization room 11, ammonia nitrogen removal room 12 and total nitrogen
Room 13 is removed, when sewage is flowed into the sewage-treatment plant 10, phosphorus, ammonia nitrogen and the total nitrogen in sewage can be removed,
So as to once remove the multiple element in sewage, asked the need for meeting user.The present invention is by the dephosphorization room 11, ammonia in addition
Nitrogen removes room 12 and total nitrogen removes and sewage disposal filler is filled with room 13, therefore sewage can only be penetrated through slowly successively
Dephosphorization room 11, ammonia nitrogen removal room 12 and total nitrogen remove room 13, and sewage needs to take longer time through sewage-treatment plant 10,
Therefore sewage-treatment plant 10 can be more fully handled sewage, and then wastewater treatment efficiency is more preferable.
In order that obtain sewage transport mechanism 20 preferably can convey sewage to the sewage-treatment plant 10, herein,
Preferably, the sewage transport mechanism 20 is a sewage conveying tube for being arranged at the top of sewage-treatment plant 10.Therefore it is dirty
Water delivery pipe can be directly from the sewage-treatment plant 10 top spray sewage downwards, sewage is during flowing downward
It can be mixed with air and increase the oxygen content in air.
In order to further increase the content oxygen in sewage, herein, the water outlet of the sewage conveying tube is provided with one
The atomizer 21 that sewage can be atomized.Due in the present embodiment, again from dirt after using atomizer 21, sewage is atomized
The top of water treatment facilities 10 is sprayed in the sewage-treatment plant 10, in the process, increases connecing for sewage and air
Contacting surface is accumulated, and then greatly increases the oxygen content of sewage, in order to which follow-up microorganism is reacted and eliminated in sewage to it
Various elements, and then make it that the treatment effect of sewage is more preferable.
Herein, for the ease of removing the P elements of sewage, while reducing being produced into for the sewage disposal system of the present invention
This, it is preferable that sponge iron, manganese sand, organic matter degradation bacterium and polyP bacteria are filled with the dephosphorization room 11.
In order that organic matter degradation bacterium in dephosphorization room 11 and polyP bacteria preferably react with sewage, in this implementation
In example, the turner structure 110 of upset filler is additionally provided with the dephosphorization room 11, the turner structure 110 is set including an activity
Multiple turn over is provided with the rotary shaft being placed in the dephosphorization room 11, the rotary shaft and throws oar 111, while rotary shaft is also associated with
The drive device for driving it to rotate, above-mentioned drive device is preferably motor, and engine or rotary cylinder etc. are alternatively certainly.
By being provided with turner structure 110 in dephosphorization room 11, the turner structure 110 can constantly overturn filler, and then to fill out
Material can be preferably with air contact, the oxygen content in increase filler, so organic matter degradation bacterium in the dephosphorization room 11 and
PolyP bacteria preferably reacts with sewage so that the phosphor-removing effect of sewage is more preferable.
In the present invention, sponge filler, graded broken stone, organic matter degradation bacterium and nitre are filled with the ammonia nitrogen removal room 12
Change bacterium.Other kind of sewage disposal filler is filled in certain ammonia nitrogen removal room 12 also possible, with specific reference to actual need
Depending on wanting.
As in a preferred embodiment of the present invention, the total nitrogen removes then thin filled with pelelith, denitrification in room 13
Bacterium, corncob and bio-based materials.Herein, described bio-based materials are preferably polyhydroxyalkanoate, above-mentioned biology
Sill can also be not limited to polyhydroxyalkanoate using other materials.Certainly remove in room 13 can be with for the total nitrogen
Fill other sewage disposal fillers.
In order to which the impurity in sewage can be removed, herein, it is preferable that the ammonia nitrogen removal room 12 and total nitrogen remove room 13
Between be additionally provided with a filter chamber 14, the filter chamber 14 be filled with rubble.It is dirty by den of monsters filter chamber 14 of institute filtering precipitation
Impurity in water, and then make it that the treatment effect of sewage is more preferable.
Wherein, in order to can preferably into the dephosphorization room 11, ammonia nitrogen removal room 12 supplemental oxygen, herein, preferably
Ground, the dephosphorization room 11, ammonia nitrogen removal room 12 and filter chamber 14 are cascadingly set on the dirt along direction from top to bottom
In the inside of water treatment facilities 10, the bottom of the filter chamber 14 is additionally provided with aeration tube 140, therefore aeration tube 140 is described in
When being aerated in filter chamber 14, gas can be raised above and sequentially enter ammonia nitrogen removal room 12 and the dephosphorization room 11, and then be institute
State dephosphorization room 11, the supplemental oxygen of ammonia nitrogen removal room 12.
The preferred embodiments of the present invention are the foregoing is only, as long as realizing the skill of the object of the invention with essentially identical means
Art scheme is belonged within protection scope of the present invention.
Claims (8)
1. a kind of osmosis system applied to sewage disposal, including：
One sewage-treatment plant (10),
One sewage transport mechanism (20)；The sewage transport mechanism (20) is used for pending to the sewage-treatment plant (10) conveying
Sewage；
It is characterized in that：
The sewage-treatment plant (10) is internally provided with dephosphorization room (11), ammonia nitrogen removal room (12) and total nitrogen and removes room (13),
The dephosphorization room (11), ammonia nitrogen removal room (12) and total nitrogen, which are removed, is filled with sewage disposal filler in room (13)；
The sewage transport mechanism (20) enters sewage transport in the sewage-treatment plant (10), and sewage flows successively passes through institute
Dephosphorization room (11), ammonia nitrogen removal room (12) and total nitrogen are stated and have removed room (13)；
The turner structure (110) of upset filler is additionally provided with the dephosphorization room (11), the turner structure (110) includes one and lived
Multiple turn over is provided with the dynamic rotary shaft being arranged in the dephosphorization room (11), the rotary shaft and throws oar (111).
2. a kind of osmosis system applied to sewage disposal according to claim 1, it is characterised in that：
The sewage transport mechanism (20) is a sewage conveying tube being arranged above the sewage-treatment plant (10).
3. a kind of osmosis system applied to sewage disposal according to claim 1, it is characterised in that：
Sponge iron, manganese sand, organic matter degradation bacterium and polyP bacteria are filled with the dephosphorization room (11).
4. a kind of osmosis system applied to sewage disposal according to claim 1, it is characterised in that：
Sponge filler, graded broken stone, organic matter degradation bacterium and nitrobacteria are filled with the ammonia nitrogen removal room (12).
5. a kind of osmosis system applied to sewage disposal according to claim 1, it is characterised in that：
The total nitrogen, which is removed, is filled with pelelith, denitrifying bacteria, corncob and bio-based materials in room (13).
6. a kind of osmosis system applied to sewage disposal according to claim 1, it is characterised in that：
The ammonia nitrogen removal room (12) and total nitrogen are additionally provided with a filter chamber (14), the filter chamber (14) between removing room (13)
In be filled with rubble.
7. a kind of osmosis system applied to sewage disposal according to claim 6, it is characterised in that：
The dephosphorization room (11), ammonia nitrogen removal room (12) and filter chamber (14) are cascadingly set on along direction from top to bottom
In the inside of the sewage-treatment plant (10).
8. a kind of osmosis system applied to sewage disposal according to claim 6 or 7, it is characterised in that：
The bottom of the filter chamber (14) is additionally provided with aeration tube (140).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710374365.4A CN107055815A (en) | 2017-05-24 | 2017-05-24 | A kind of osmosis system applied to sewage disposal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710374365.4A CN107055815A (en) | 2017-05-24 | 2017-05-24 | A kind of osmosis system applied to sewage disposal |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107055815A true CN107055815A (en) | 2017-08-18 |
Family
ID=59609717
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710374365.4A Pending CN107055815A (en) | 2017-05-24 | 2017-05-24 | A kind of osmosis system applied to sewage disposal |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107055815A (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102617002A (en) * | 2012-04-16 | 2012-08-01 | 温州大学 | Method for treating dispersed domestic sewage |
| CN102674631A (en) * | 2012-05-10 | 2012-09-19 | 复旦大学 | Method and system for advanced treatment of centralized rural domestic sewage |
| CN103121754A (en) * | 2011-11-18 | 2013-05-29 | 上海市政工程设计研究总院（集团）有限公司 | Denitrification and dephosphorization technique |
-
2017
- 2017-05-24 CN CN201710374365.4A patent/CN107055815A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103121754A (en) * | 2011-11-18 | 2013-05-29 | 上海市政工程设计研究总院（集团）有限公司 | Denitrification and dephosphorization technique |
| CN102617002A (en) * | 2012-04-16 | 2012-08-01 | 温州大学 | Method for treating dispersed domestic sewage |
| CN102674631A (en) * | 2012-05-10 | 2012-09-19 | 复旦大学 | Method and system for advanced treatment of centralized rural domestic sewage |
Non-Patent Citations (2)
| Title |
|---|
| 全国勘察设计注册工程师环保专业管理委员会: "《注册环保工程师专业考试复习教材 水污染防治工程技术与实践》", 31 March 2017, 中国环境出版社 * |
| 陈赛花: "《探索微观世界的精灵 细菌与人类》", 31 January 2012, 上海科学普及出版社 * |
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| PB01 | Publication | ||
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| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170818 |