CN106277636A - A kind of sewage purification processing system - Google Patents
A kind of sewage purification processing system Download PDFInfo
- Publication number
- CN106277636A CN106277636A CN201610819488.XA CN201610819488A CN106277636A CN 106277636 A CN106277636 A CN 106277636A CN 201610819488 A CN201610819488 A CN 201610819488A CN 106277636 A CN106277636 A CN 106277636A
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- China
- Prior art keywords
- reaction
- inner core
- cylinder
- sewage
- urceolus
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- 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.)
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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
-
- 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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- 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
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- 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)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The invention discloses a kind of sewage purification processing system, including chemical reaction cylinder, cell reaction cylinder and biofilter, described chemical reaction cylinder includes reacting urceolus, the intermediate cylinder being sequentially located in described reaction urceolus and reaction inner core, described reaction inner core is divided into two independent upper reaction inner cores and lower reaction inner core, described reaction urceolus top is provided with stirring motor, and described cell reaction cylinder includes two electrode plate being connected respectively with ground electrode and high-voltage pulse power source, is provided with filtrate in biofilter.The present invention first passes through three medicaments of interpolation in upper reaction inner core, lower reaction inner core and intermediate cylinder, medicament and sewage is made to be sufficiently mixed reaction, dirt Organic substance in water is processed, improve the treatment effeciency of sewage, improve the biodegradability of sewage, organic matter of sewage undecomposed in chemical reaction cylinder is degraded further by cell reaction cylinder the most again, degraded by the two-stage Organic substance to sewage of degrading, good degrading effect.
Description
Technical field
The present invention relates to technical field of sewage, particularly relate to a kind of sewage purification processing system.
Background technology
Classifying by sewage source, sewage disposal is generally divided into production waste and processes and sanitary sewage disposal.Production waste bag
Include trade effluent, rural sewage and medical sewage etc., and sanitary sewage is exactly the sewage that daily life produces, and refers to various shape
The inorganic matter of formula and organic complex mixture, including: the floating and size solid particle of suspension, gluey and gel spreads
Thing, and pure solution.Along with the fast development of industry, the generation of industrial wastewater is also increasing year by year, and river receives the tightest
The pollution of weight, interior river course is closely related with the life of the mankind, and the interior pollution of river is also the most serious, contains in major part industrial wastewater
Having bio-refractory Organic substance, hardly degraded organic substance is drained in interior river course and does great damage environment, thus endangers further
The health of victimization class.
The difficult degradation applying the light-catalyzed reaction of the metal-oxides such as titanium dioxide to decompose in sewage in prior art has
Machine thing, but in the metal-oxide powder Photocatalytic Degradation Process such as titanium dioxide, in easily causing reaction vessel, light radiation is obstructed, gold
Belong to the problems such as oxide powder consolidation, powder body loss, and utilize zeolite, glass, monocrystal silicon, electro-conductive glass etc. for carrying both at home and abroad
Body prepares metal-oxide composite catalyzing material, but the preparation cost of these methods is high, and granular composite material is in reaction vessel
The problem still suffering from causing light radiation to be obstructed, and there is also between bulk material friction and powdered problem, further, since need degraded
The material relative concentration in titanium dioxide powder surface is little, the photocatalytic degradation speed of the metal-oxide powders such as titanium dioxide
Slowly.
Publication No. is that the Chinese patent literature of CN105347590A discloses a kind of sewage-treatment plant, including being sequentially connected with
Prefabricated combined septic tank device, abandoned stream defecator, combined-flow defecator, device for deep cleaning and connect with device for deep cleaning
Cistern；It is provided with water inlet device in device for deep cleaning, is connected with filter vat by nozzle below water inlet device, square tube under filter vat
Cross the first water receiving bucket to be connected with filter, be connected with cyclic water tank by the second water receiving bucket below filter, cyclic water tank
Inside being provided with circulating pump, circulating pump connects circulation pipe, and the other end of circulation pipe is connected with water inlet device top side, recirculated water
Connected with cistern by water-supply-pipe below case.When using this sewage-treatment plant, sewage filters dress through dirty hanging basket device, abandoned stream
Put, the filtration successively of combined-flow defecator, device for deep cleaning enters in cistern, simple to operate, safe and reliable, repeatable
Filter, improve filter effect, but Organic substance can not be processed by this sewage filter device effectively, to dirty water purification effect
The most bad.
Summary of the invention
Based on above the deficiencies in the prior art, technical problem solved by the invention is to provide a kind of degradation speed fast,
The impurity in water outlet can be sufficiently separated, the sewage purification processing system good to wastewater purifying efficiency.
In order to solve above-mentioned technical problem, the present invention provides a kind of sewage purification processing system, including chemical reaction cylinder, electricity
Solving reaction tube and biofilter, described chemical reaction cylinder includes reacting urceolus, is sequentially located at the intermediate cylinder in described reaction urceolus
With reaction inner core, described reaction inner core is divided into two independent upper reaction inner cores and lower reaction inner core, described reaction urceolus top
Being provided with stirring motor, the shaft being connected with described stirring motor runs through described upper reaction inner core and lower reaction inner core, upper instead
It is configured with stirring vane in answering inner core and lower reaction inner core；The downside of described upper reaction inner core is provided with water inlet pipe, described upper reaction
Being provided with connecting tube between upside and the upside of lower reaction inner core of inner core, the upside another side of described lower reaction inner core is provided with water outlet
Mouthful, it being provided with outlet pipe on the upside of described intermediate cylinder, the end of described outlet pipe stretches to the bottom of reaction urceolus；Described water inlet pipe and company
Being respectively equipped with the first chemical feed pipe and the second chemical feed pipe in adapter, the downside of described intermediate cylinder is provided with the 3rd chemical feed pipe；Described reaction
The downside of urceolus and upside are respectively equipped with discharge pipeline and drain pipe；Described cell reaction cylinder include respectively with ground electrode and high pressure
Two electrode plate that the pulse power is connected, are provided with filtrate in described biofilter.
As the preferred implementation of technique scheme, the sewage purification processing system that the embodiment of the present invention provides enters one
Walk and include the part or all of of following technical characteristic:
As the improvement of technique scheme, between described cell reaction cylinder and biofilter, it is additionally provided with expansion chamber.
As the improvement of technique scheme, in one embodiment of the invention, described intermediate cylinder is supported by support
Centre position at described reaction urceolus.
As the improvement of technique scheme, set the most successively between described reaction outer tube inner wall and intermediate cylinder outer wall
Having fine straining plate and coarse filtration plate, described outlet pipe passes described fine straining plate and coarse filtration plate.
Further, described drain pipe is connected with the inlet of cell reaction cylinder, and the liquid outlet of cell reaction cylinder passes through water
Pipe is connected with described biofilter with elevator pump.
Further, the filter plate being provided with filter cap bottom described biofilter carries out water distribution.
As the improvement of technique scheme, described stirring motor is the frequency conversion motor of 22KW, and rotating speed is 75r/min.
Preferably, described filtrate is the coke granule of 3-5mm.
Compared with prior art, technical scheme has the advantages that the dirty water decontamination handles of the present invention
System first passes through the reaction urceolus in chemical reaction cylinder, intermediate cylinder and three reaction tubes of reaction inner core and processes sewage,
Intake in the downside of upper reaction inner core by water inlet pipe, can realize flowing up of sullage rotational flow, and upper reaction inner core, lower instead
Answer in inner core and intermediate cylinder three medicaments of interpolation, make medicament and sewage be sufficiently mixed reaction, the present invention upper reaction inner core and under
It is configured with stirring vane in reaction inner core, when sewage is in upper reaction inner core and lower reaction inner core, the stirring vane dirt to process
Water is stirred, it is ensured that form the state of flowing between sewage and medicament, and sewage is fully contacted with medicament, it is ensured that sewage and medicament
Abundant reaction, produce precipitation, dirt Organic substance in water processed, improve the treatment effeciency of sewage, raising sewage can
Biochemical, there is non-resilient touching in the hard-degraded substance contained the most again by the cell reaction cylinder a large amount of high energy electrons of generation and sewage
Hit, energy is converted into the interior energy of ground state molecule, excite, dissociate and a series of processes such as ionization, make sewage be in activation
State, on the one hand the energy of generation is opened organic matter of sewage molecular link, is produced some simple substance atom or monoatomic molecules, the opposing party
Face produces substantial amounts of free oxygen, free radical and ozone isoreactivity group, and the ozone produced in chemical reaction cylinder also can contain
Stay in sewage, organic matter of sewage undecomposed in chemical reaction cylinder is degraded further, is degraded by two-stage right
The Organic substance of sewage is degraded, good degrading effect, and sewage purification processing system of the present invention passes through during whole degraded
Elevator pump controls the flow velocity of sewage, and whole degradation process speed is fast, and by purification further to sewage in biofilter, this
The wastewater purifying efficiency of bright sewage purification processing system is good.
Described above is only the general introduction of technical solution of the present invention, in order to better understand the technological means of the present invention,
And can be practiced according to the content of description, and in order to allow the above and other objects, features and advantages of the present invention can
Become apparent, below in conjunction with preferred embodiment, and coordinate accompanying drawing, describe in detail as follows.
Accompanying drawing explanation
In order to be illustrated more clearly that the technical scheme of the embodiment of the present invention, the accompanying drawing of embodiment will be situated between simply below
Continue.
Fig. 1 is the structural representation of the sewage purification processing system of the preferred embodiment of the present invention.
Reference: 10, chemical reaction cylinder；11, reaction urceolus；111, fine straining plate；112, coarse filtration plate；113, support；12、
Intermediate cylinder；121, the 3rd chemical feed pipe；13, reaction inner core；131, upper reaction inner core；132, lower reaction inner core；133, outlet；
14, stirring motor；141, shaft；142, stirring vane；15, water inlet pipe；151, the first chemical feed pipe；16, connecting tube；161,
Two chemical feed pipes；17, outlet pipe；18, discharge pipeline；19, drain pipe；20, cell reaction cylinder；21, battery lead plate；22, inlet；23、
Liquid outlet；30, biofilter；31, filtrate；32, filter plate；40, expansion chamber；50, water pipe；51, elevator pump.(note: Fig. 1 is left
Detailed description of the invention
Describing the detailed description of the invention of the present invention below in conjunction with the accompanying drawings in detail, it, as the part of this specification, passes through
Embodiment illustrates the principle of the present invention, and other aspects of the present invention, feature and advantage thereof will be become by this detailed description
Very clear.In the accompanying drawing of institute's reference, in different figures, same or analogous parts use identical drawing reference numeral to represent.
As it is shown in figure 1, be the sewage purification processing system schematic diagram of the preferred embodiment of the present invention, the preferred embodiment of the present invention
Sewage purification processing system include chemical reaction cylinder 10, cell reaction cylinder 20 and biofilter 30, chemical reaction cylinder 10 includes
Reaction urceolus 11, the intermediate cylinder 12 being sequentially located in described reaction urceolus 11 and reaction inner core 13, it is preferable that described intermediate cylinder 12
The centre position of described reaction urceolus 11 it is supported on by support 113.Described reaction inner core 13 is divided into two independent upper reactions
Inner core 131 and lower reaction inner core 132, described reaction urceolus 11 top is provided with stirring motor 14, is connected with described stirring motor 14
Shaft 141 run through described upper reaction inner core 131 and lower reaction inner core 132, at upper reaction inner core 131 and lower reaction inner core
Being configured with stirring vane 142 in 132, described stirring vane 142 is fixed on described shaft 141；Described upper reaction inner core 131
Downside be provided with water inlet pipe 15, be provided with connecting tube between upside and the upside of lower reaction inner core 132 of described upper reaction inner core 131
16, the upside another side of described lower reaction inner core 132 is provided with outlet 133, is provided with outlet pipe 17, institute on the upside of described intermediate cylinder 12
The end stating outlet pipe 17 stretches to the bottom of reaction urceolus 11, and described outlet pipe 17 is provided with two altogether, is divided into intermediate cylinder 12
The left and right sides.Be respectively equipped with the first chemical feed pipe 151 and the second chemical feed pipe 161 on described water inlet pipe 15 and connecting tube 16, described in
Between the downside of cylinder 12 be provided with the 3rd chemical feed pipe 121；The downside of described reaction urceolus 11 and upside are respectively equipped with discharge pipeline 18 and row
Water pipe 19.
Described cell reaction cylinder 20 includes two electrode plate 21 being connected respectively with ground electrode and high-voltage pulse power source,
There is non-resilient touching in the hard-degraded substance that high-voltage pulse power source is contained by the battery lead plate electric discharge a large amount of high energy electrons of generation and sewage
Hit, energy is converted into the interior energy of ground state molecule, excite, dissociate and a series of processes such as ionization, make sewage be in activation
State, on the one hand the energy of generation is opened organic matter of sewage molecular link, is produced some simple substance atom or monoatomic molecules, the opposing party
Face produces substantial amounts of free oxygen, free radical and ozone isoreactivity group, and combining electrolysis in cell reaction cylinder 20 can be the most right
The hardly degraded organic substance of sewage is degraded.The active grain being made up of these monoatomic molecules, free oxygen free radical and ozone etc.
Chemical reaction caused by son, the complicated macromolecule contaminant in sewage is changed into simple small-molecule substance the most at last, and can make
Venomous injurant in sewage is changed into nontoxic material or the removal so that pollutant are degraded of low toxicity low pest matter.
The sewage-treatment plant of the present invention uses and imports sewage in the downside of upper reaction inner core 131, and then eddy flow ground is upwards
It is full of upper reaction inner core 131, makes sewage and medicament just can be sufficiently mixed reaction in initial reaction stage, through the sewage of first set reaction
Enter into lower reaction inner core 132 by connecting tube 16, again add medicament by the second chemical feed pipe 161, at lower reaction inner core 132
In carry out second time react, in upper reaction inner core 131 and lower reaction inner core 132, be provided with stirring vane 142, at stirring motor
14 and shaft 141 effect under promote sewage and medicament more fully to react.Reacted dirt in reaction inner core 13
Water enters into intermediate cylinder 12 from the outlet 133 of lower reaction inner core 132, by the 3rd chemical feed pipe 121 to the dirt in intermediate cylinder 12
Water carries out third time adding medicine, sewage and medicament secondary response again, and then the outlet pipe 17 on the upside of intermediate cylinder 12 enters into reaction
Urceolus 11, carries out the sewage after third-order reaction and forms precipitation, accumulate the bottom at reaction urceolus 11, along with in reaction urceolus 11
Water level constantly raises, and the water purified through chemical reaction cylinder 10 flows to cell reaction cylinder 20 from the drain pipe 19 reacted on the upside of urceolus 11
In, and the discharge pipeline 18 that the precipitate in sewage is on the downside of reaction urceolus 11 is discharged.
Preferably, described stirring motor 14 is the frequency conversion motor of 22KW, and rotating speed is 75r/min, is carried by stirring motor 14
Dynamic shaft 141 rotates, and then is stirred the sewage in reaction inner core 13, so that medicament uniformly mixes with sewage, and reaction
Fully.
Further, fine straining plate it is sequentially provided with from top to bottom between described reaction urceolus 11 inwall and intermediate cylinder 12 outer wall
111 and coarse filtration plate 112, described outlet pipe 17 is through described fine straining plate 111 and coarse filtration plate 112, after sewage and medicament fully react,
Pass sequentially through coarse filtration plate 112 and fine straining plate 111, filter out the silt containing smaller particle and float, improve dirty water purification
Rate.
It addition, be provided with filtrate 31 in described biofilter 30, bottom described biofilter 30, it is provided with the filter plate of filter cap
32 carry out water distribution, and described filtrate 31 uses the coke granule of 3-5mm, make after chemical reaction cylinder 10 and cell reaction cylinder 20 decompose
Sewage purified further in biofilter 30.
Further, between described cell reaction cylinder 20 and biofilter 30, it is additionally provided with expansion chamber 40, to through purifying
Water carry out settlement treatment.
Concrete, described drain pipe 19 is connected with the inlet 22 of cell reaction cylinder 20, the liquid outlet of cell reaction cylinder 20
23 are connected with described biofilter 30 with elevator pump 51 by water pipe 50.
The sewage purification processing system that the present invention proposes first passes through the reaction urceolus 11 in chemical reaction cylinder 10, intermediate cylinder
Sewage is processed by 12 with reaction 13 3 reaction tubes of inner core, is intake in the downside of upper reaction inner core 131 by water inlet pipe 15,
Flowing up of sullage rotational flow can be realized, and add three times in upper reaction inner core 131, lower reaction inner core 132 and intermediate cylinder 12
Medicament, makes medicament and sewage be sufficiently mixed reaction, and the present invention is configured with in upper reaction inner core 131 and lower reaction inner core 132 and stirs
Mixing blade 142, when sewage is in upper reaction inner core 131 and lower reaction inner core 132, the sewage of process is carried out by stirring vane 142
Stirring, it is ensured that forming the state of flowing between sewage and medicament, sewage is fully contacted with medicament, it is ensured that sewage is abundant with medicament
Reaction produces precipitation, is processed by dirt Organic substance in water, improves the treatment effeciency of sewage, improves the biodegradability of sewage,
The hard-degraded substance generation inelastic collision that a large amount of high energy electron contains is produced with sewage the most again by cell reaction cylinder 20, will
Energy is converted into the interior energy of ground state molecule, excites, dissociates and a series of processes such as ionization, makes sewage be in the state of activation,
On the one hand the energy produced opens organic matter of sewage molecular link, produces some simple substance atom or monoatomic molecules, on the other hand produces
Raw substantial amounts of free oxygen, free radical and ozone isoreactivity group, and the ozone produced in chemical reaction cylinder also can contain and stay
In sewage, organic matter of sewage undecomposed in chemical reaction cylinder 10 is degraded further, is degraded to dirt by two-stage
The Organic substance of water is degraded, good degrading effect, and sewage purification processing system of the present invention passes through to carry during whole degraded
Rising pump 51 and control the flow velocity of sewage, whole degradation process speed is fast, and by purification further to sewage in biofilter 30, this
The wastewater purifying efficiency of the sewage purification processing system of invention is good.
The above is the preferred embodiment of the present invention, certainly can not limit the right model of the present invention with this
Enclose, it is noted that for those skilled in the art, under the premise without departing from the principles of the invention, also may be used
To make some improvement and variation, these improve and variation is also considered as protection scope of the present invention.
Claims (5)
1. a sewage purification processing system, including chemical reaction cylinder (10), cell reaction cylinder (20) and biofilter (30), its
It is characterised by: described chemical reaction cylinder (10) includes reacting urceolus (11), is sequentially located at the centre in described reaction urceolus (11)
Cylinder (12) and reaction inner core (13), in described reaction inner core (13) is divided into two independent upper reaction inner cores (131) and lower reaction
Cylinder (132), described reaction urceolus (11) top is provided with stirring motor (14), the shaft being connected with described stirring motor (14)
(141) described upper reaction inner core (131) and lower reaction inner core (132) are run through, at upper reaction inner core (131) and lower reaction inner core
(132) stirring vane (142) it is configured with in；The downside of described upper reaction inner core (131) is provided with water inlet pipe (15), described upper reaction
Connecting tube (16), described lower reaction inner core (132) it is provided with between upside and the upside of lower reaction inner core (132) of inner core (131)
Upside another side be provided with outlet (133), described intermediate cylinder (12) upside is provided with outlet pipe (17), described outlet pipe (17)
End stretches to the bottom of reaction urceolus (11)；It is respectively equipped with the first chemical feed pipe on described water inlet pipe (15) and connecting tube (16)
(151) and the second chemical feed pipe (161), the downside of described intermediate cylinder (12) is provided with the 3rd chemical feed pipe (121)；Described reaction urceolus
(11) downside and upside are respectively equipped with discharge pipeline (18) and drain pipe (19)；Described cell reaction cylinder (20) include respectively with connect
Two electrode plate (21) that ground electrode is connected with high-voltage pulse power source, are provided with filtrate (31) in described biofilter (30),
Be additionally provided with expansion chamber (40) between described cell reaction cylinder (20) and biofilter (30), described reaction urceolus (11) inwall and in
Between be sequentially provided with fine straining plate (111) and coarse filtration plate (112) from top to bottom between cylinder (12) outer wall, described outlet pipe (17) passes institute
State fine straining plate (111) and coarse filtration plate (112).
2. sewage purification processing system as claimed in claim 1, it is characterised in that: described intermediate cylinder (12) passes through support
(113) centre position of described reaction urceolus (11) it is supported on.
3. sewage purification processing system as claimed in claim 1, it is characterised in that: described drain pipe (19) and cell reaction cylinder
(20) inlet (22) is connected, and the liquid outlet (23) of cell reaction cylinder (20) passes through water pipe (50) and elevator pump (51) with described
Biofilter (30) is connected.
4. sewage purification processing system as claimed in claim 1, it is characterised in that: described biofilter (30) bottom is provided with
Filter plate (32) with filter cap carries out water distribution.
5. sewage purification processing system as claimed in claim 1, it is characterised in that: described filtrate (31) is the coke of 3-5mm
Granule.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610819488.XA CN106277636A (en) | 2016-09-13 | 2016-09-13 | A kind of sewage purification processing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610819488.XA CN106277636A (en) | 2016-09-13 | 2016-09-13 | A kind of sewage purification processing system |
Publications (1)
| Publication Number | Publication Date |
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| CN106277636A true CN106277636A (en) | 2017-01-04 |
Family
ID=57710008
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201610819488.XA Withdrawn CN106277636A (en) | 2016-09-13 | 2016-09-13 | A kind of sewage purification processing system |
Country Status (1)
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Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101746923A (en) * | 2009-08-19 | 2010-06-23 | 赵立功 | Coking wastewater deep treatment and reuse process and equipment thereof |
| CN101863589A (en) * | 2010-06-09 | 2010-10-20 | 中国海洋石油总公司 | Method for advanced treatment of wastewater by using combination of catalytic ozonation and internal circulation biological filter |
| CN102936083A (en) * | 2012-11-14 | 2013-02-20 | 北京赛科康仑环保科技有限公司 | Device and method for removing refractory organics and total nitrogen in waste water simultaneously |
| CN204689695U (en) * | 2015-03-20 | 2015-10-07 | 涂智 | A kind of waste disposal plant |
| CN205368033U (en) * | 2015-12-29 | 2016-07-06 | 广东卓信环境科技股份有限公司 | Bological aerated filter integrative device of disposing of sewage |
-
2016
- 2016-09-13 CN CN201610819488.XA patent/CN106277636A/en not_active Withdrawn
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101746923A (en) * | 2009-08-19 | 2010-06-23 | 赵立功 | Coking wastewater deep treatment and reuse process and equipment thereof |
| CN101863589A (en) * | 2010-06-09 | 2010-10-20 | 中国海洋石油总公司 | Method for advanced treatment of wastewater by using combination of catalytic ozonation and internal circulation biological filter |
| CN102936083A (en) * | 2012-11-14 | 2013-02-20 | 北京赛科康仑环保科技有限公司 | Device and method for removing refractory organics and total nitrogen in waste water simultaneously |
| CN204689695U (en) * | 2015-03-20 | 2015-10-07 | 涂智 | A kind of waste disposal plant |
| CN205368033U (en) * | 2015-12-29 | 2016-07-06 | 广东卓信环境科技股份有限公司 | Bological aerated filter integrative device of disposing of sewage |
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Application publication date: 20170104 |