CN106007267A - Large integrated sewage treatment device and sewage treatment technology - Google Patents
Large integrated sewage treatment device and sewage treatment technology Download PDFInfo
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- CN106007267A CN106007267A CN201610624436.7A CN201610624436A CN106007267A CN 106007267 A CN106007267 A CN 106007267A CN 201610624436 A CN201610624436 A CN 201610624436A CN 106007267 A CN106007267 A CN 106007267A
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- sewage
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- contact
- oxidation pool
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- 239000010865 sewage Substances 0.000 title claims abstract description 76
- 238000005516 engineering process Methods 0.000 title abstract description 8
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 42
- 238000004062 sedimentation Methods 0.000 claims abstract description 31
- 239000007788 liquid Substances 0.000 claims abstract description 26
- 230000001105 regulatory effect Effects 0.000 claims abstract description 25
- 239000010802 sludge Substances 0.000 claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000000945 filler Substances 0.000 claims abstract description 19
- 238000006065 biodegradation reaction Methods 0.000 claims abstract description 4
- 238000001914 filtration Methods 0.000 claims abstract description 3
- 238000000034 method Methods 0.000 claims description 17
- 238000010992 reflux Methods 0.000 claims description 10
- 239000007789 gas Substances 0.000 claims description 9
- 239000000126 substance Substances 0.000 claims description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 7
- 239000001301 oxygen Substances 0.000 claims description 7
- 229910052760 oxygen Inorganic materials 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 4
- 238000000746 purification Methods 0.000 claims description 3
- 239000002244 precipitate Substances 0.000 claims description 2
- 238000005086 pumping Methods 0.000 claims description 2
- 230000003647 oxidation Effects 0.000 abstract description 7
- 244000005700 microbiome Species 0.000 abstract description 2
- 238000007599 discharging Methods 0.000 abstract 1
- 239000011259 mixed solution Substances 0.000 abstract 1
- 239000002351 wastewater Substances 0.000 description 6
- 239000003643 water by type Substances 0.000 description 4
- 238000005273 aeration Methods 0.000 description 3
- 238000005276 aerator Methods 0.000 description 3
- 230000032683 aging Effects 0.000 description 3
- 238000010276 construction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000003911 water pollution Methods 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 206010002660 Anoxia Diseases 0.000 description 1
- 241000976983 Anoxia Species 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- 206010028980 Neoplasm Diseases 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- RSWGJHLUYNHPMX-ONCXSQPRSA-N abietic acid Chemical compound C([C@@H]12)CC(C(C)C)=CC1=CC[C@@H]1[C@]2(C)CCC[C@@]1(C)C(O)=O RSWGJHLUYNHPMX-ONCXSQPRSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000007953 anoxia Effects 0.000 description 1
- 230000001458 anti-acid effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000003139 buffering effect Effects 0.000 description 1
- 208000035269 cancer or benign tumor Diseases 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 210000005056 cell body Anatomy 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000005553 drilling Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 230000002503 metabolic effect Effects 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000006213 oxygenation reaction Methods 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 210000003437 trachea Anatomy 0.000 description 1
- 230000003442 weekly effect Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—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
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/007—Contaminated open waterways, rivers, lakes or ponds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Sludge (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
The invention discloses a large integrated sewage treatment device and a sewage treatment technology. The device comprises: a grid, a regulating tank, an anaerobic tank, a contact oxidation tank, a sedimentation tank, a sludge tank, a fan chamber and an equipment room. The technology consists of: filtering sewage through the grid and then letting the sewage enter the regulating tank; when the regulating tank liquid level reaches a high liquid level set by a liquid level floating ball, starting a lifting pump automatically to send sewage into the anaerobic tank, using elastic filler as the carrier of anaerobic microorganisms and carrying out anaerobic biodegradation; making the sewage flow into the contact oxidation tank through an anaerobic tank overflow port, the degraded and purified sewage and sludge mixed solution flows into the sedimentation tank through the contact oxidation tank overflow port, carrying out sedimentation in the sedimentation tank, and discharging the up-to-standard sewage into a riverway through a drain pipe. According to the invention, the device can be constructed in a riverway water area, and the technology provided by the invention, and the device and the technology have the advantages of thorough sewage treatment and the like.
Description
Technical field
The present invention relates to sewage treatment area, particularly relate at large-scale integrated sewage treating apparatus and sewage
Science and engineering skill.
Background technology
China's water pollution problem is the severeest at present.The particularly water pollution in city below two wires is suitable
Seriously.And these water pollutions arch-criminal be exactly large-scale polluter waters or administer halfway waters to
River course is drained, causes waters, river course to need to put into substantial amounts of manpower and materials and administer, and also can not get showing
The regulation effect write.Therefore, the sewage discharged for city below two wires carries out integrating improvement, and administers
Equipment investment and operation cost is low and sewage disposal is thorough, is only key point.
City below two wires the most concern is the Cost Problems of waste water control.And rely on current waste water control
Technology, if wanting to improve greatly the effect of waste water control on the basis of reducing cost, increases sewage disposal
The volume of equipment is one of good method.And to increase the volume of equipment, the building sides on ground will be increased
Long-pending.Although now many sewage disposal devices can be imbedded in underground, but the vertical earth's surface of equipment region, depend on
So cannot carry weight, and equipment easily corrodes, and the later stage is because sewage and mud after processing need equipment
Transport to ground, this adds increased the operation cost in later stage.The present invention is at the river course water surface of blowdown by equipment construction,
This just can solve problem above.
Summary of the invention
It is an object of the invention to provide that one can in waters, river course and sewage disposal be thorough by plant construction
The large-scale integrated sewage treating apparatus at the end and sewage treatment process.
The present invention solves the scheme that its technical problem is used: large-scale integrated sewage treating apparatus, including
Grid, regulating reservoir, anaerobic pond, contact-oxidation pool, sedimentation tank, sludge-tank, fan house, canyon, described
Grids top is connected with sewage pipe, and described regulating reservoir is wrapped in grid, and described liquid-level floater is positioned at regulating reservoir
Portion, described elevator pump is positioned at bottom regulating reservoir, and described water pipe one end is connected with regulating reservoir, the other end and anaerobic pond
Connecting, described anaerobic pond is internal arranges elastic filler, and described anaerobic pond manhole is positioned at anaerobic pond top, described in detest
Oxygen pond overfall is positioned at anaerobic pond upper side and connects contact-oxidation pool, described contact-oxidation pool lower disposed cloth
Trachea, described gas distribution pipe is arranged rotary mixing aerator, and described gas distribution pipe is by airduct and the wind within fan house
Machine connects, and described contact-oxidation pool is internal arranges elastic filler, and described contact-oxidation pool manhole is positioned at catalytic oxidation
Top, pond, described contact-oxidation pool overfall is positioned at contact-oxidation pool upper side and connects sedimentation tank, described heavy
Swash plate is arranged on top, pond, shallow lake, and described sedimentation tank manhole is positioned at sedimentation tank top, and described discharge outlet is positioned on sedimentation tank
Side, portion is communicated to river course by drain pipe, arranges reflux pump and sludge pump, described backflow bottom described sedimentation tank
Pump is connected with contact-oxidation pool by sludge pipe, and described sludge pump is connected with sludge-tank by sludge pipe, described dirt
Mud sump top layout sludge-tank manhole, described canyon is by circuit and the liquid-level floater in regulating reservoir and lifting
Blower fan in pump, the reflux pump detested in sedimentation tank and sludge pump, fan house connects.
Described regulating reservoir, anaerobic pond, contact-oxidation pool, sedimentation tank, sludge-tank, fan house, canyon
All of wall surface is coated with anticorrosive materials.
The most significant end of described anaerobic pond overfall is less than the least significant end of contact-oxidation pool overfall.
The sewage treatment process of the large-scale integrated sewage treating apparatus of the described present invention is as follows:
Sewage, is entered in regulating reservoir by dispatch to grid by sewage pipe after the filtration of grid；
When regulating reservoir liquid level reaches the high level of liquid-level floater setting, elevator pump starts automatically, and sewage is delivered to anaerobic pond
In, when liquid level drops to the low liquid level of liquid-level floater setting, elevator pump is automatically stopped；When the boosted pumping of sewage
To anaerobic pond, anaerobe, with elastic filler as carrier, carries out anaerobic biodegradation；Sewage is through anaerobic pond
Overfall is flowed in contact-oxidation pool, and in sewage, major part Organic substance is degraded at this and purifies；Degraded and
Sewage after purification and mud mixed liquid are flowed in sedimentation tank through contact-oxidation pool overfall, precipitate through sedimentation tank
After, sewage up to standard is discharged in river course by drain pipe, and a mud part drains into contact oxygen by reflux pump
Changing in pond, another part is drained in sludge-tank by sludge pump；When concentrating full mud in sludge-tank, can borrow
Help external device to pass through sludge-tank manhole to be discharged by mud.
Beneficial effects of the present invention is as follows:
1, equipment is not take up land surface.Although equipment volume is relatively big, but equipment is arranged on river course,
It is not take up existing land area, and then also reduces construction totle drilling cost.
2, sewage load is big and processes thoroughly.The bulky advantage of this equipment utilization, can be the most right
Substantial amounts of sewage processes, and this device interior have employed high-performance bio elastic filler simultaneously, aerobic by filler
Bacterium biofilm is reacted, and based on the biomembrane being attached on carrier, through being fully contacted reaction, improves reaction efficiency
And degree of purification.
3, non-leakage, tightness is good.This invention integration makes, free from flaw, ne-leakage.
4, durable in use.Appearance uses 6mm steel plate to add Colophonium double layer anticorrosive, and compliant materials development is taken advantage of a favourable situation,
It is difficult to aging, indeformable, antiacid alkali, corrosion-resistant, eliminate traditional wastewater pond and be not suitable with the situation of sour water.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Fig. 2 is the process chart of the present invention.
In its figure: 1-sewage pipe, 2-grid, 3-regulating reservoir, 4-liquid-level floater, 5-elevator pump, 6-
Water pipe, 7-anaerobic pond, 8-anaerobic pond overfall, 9-anaerobic pond manhole, 10-contact-oxidation pool, 11-rotary mixing type
Aerator, 12-gas distribution pipe, 13-fan house, 14-elastic filler, 15-contact-oxidation pool overfall, 16-connect
Touch oxidation pond manhole, 17-canyon, 18-sedimentation tank, 19-swash plate, 20-reflux pump, 21-sludge pipe, 22-
Sludge pump, 23-discharge outlet, 24-electromagnetic valve, 25-drain pipe, 26-sedimentation tank manhole, 27-sludge-tank, 28-
Sludge-tank manhole, 29-river course, 30-blower fan.
Detailed description of the invention
1 and Fig. 2 the present invention is described in detail with specific embodiment below in conjunction with the accompanying drawings.
Setting artificial grid 2 in described grid 2, sewage introduces grid 2 well through sewage pipe 1, filters
Rear entrance sewage disposal system is uniformly processed.Grid 2 Main Function is to retain the bulk float in sewage and drift
Float, to ensure the safety of whole system plant equipment.Grid 2 is cleared up the most weekly once.
Being provided with liquid-level floater 4 and elevator pump 5 in described regulating reservoir 3, the sewage filtered through grid 2 enters
Entering in regulating reservoir 3, regulating reservoir 3 mainly stores sewage, and has the function of regulating pondage water quality, works as tune
Joint pond 3 liquid level reaches elevator pump 5 self-starting during the high level of liquid-level floater 4 setting, when liquid level drops to liquid level
Elevator pump 5 self-stopping technology during the low liquid level that ball float 4 is arranged.The Main Function of regulating reservoir 3 has 2 points: one is regulation
The water yield, buffering production line draining peak amount, provide stable service condition for follow-up sewage disposal system；Two is to examine
Considering and there are differences because of sequential difference to the pollutant levels contained by draining, equilibrium enters follow-up sewage disposal system
Sewage quality, eases off the pressure for subsequent treatment.
Described anaerobic pond 7 is built with elastic filler 14, and the boosted pump of sewage 5 carries to anaerobic pond 7,
Anaerobe, with elastic filler 14 as carrier, carries out anaerobic biodegradation, is divided by macromole complexity Organic substance
Solution becomes the labile material of little molecule to process for easy-to-keep biological provides support.Anaerobic bio-treated is as utilizing anaerobism
Property microorganism metabolic characteristic, provide under conditions of external source energy, to be reduced Organic substance as by hydrogen not needing
Body, has the methane gas of energy value simultaneously.Anaerobic biotreatment method is applicable not only to the organic dirt of high concentration
Water, water inlet BOD maximum concentration is up to tens thousand of milligrams per liter, it is possible to be applicable to low-concentration organic wastewater, such as city
Sewage etc..Anaerobic bio-treated process energy consumption is low；Organic volumetric loading is high, generally 5～10kgCOD/m3.d；
Surplus sludge volume is few；Anaerobe is low to nutritional need, resistance to poison is strong, degradable organic matter molecular mass high；Resistance to
Impact load ability is strong；The biogas of output is a kind of clean energy resource.
Hanging with elastic filler 14 in described contact-oxidation pool 10, sewage is flowed into through anaerobic pond overfall 8
In contact-oxidation pool 10, total residence time is more than 4 hours, and in sewage, major part Organic substance is dropped at this
Solving and purify, aerobic microbiological is with filler as carrier, and utilizing the Organic substance in sewage is food, by sewage
Organic substance resolves into inorganic salts and water, thus reaches the purpose purified.Contact-oxidation pool 10 air is by blower fan
30 provide.Using novel elastic filler 14 in pond, this filling surface is long-pending big, and service life is long, easy to be filmed,
Corrosion-resistant.Using rotary mixing aerator 11 at the bottom of pond, the rate of transform making dissolved oxygen is high, has lightweight, no simultaneously
Aging, be not easily blocked, service life the advantage such as length.Contact-oxidation pool 10 steam-water ratio is at 12:1, at biochemistry
In pond, interior circulation, contacts with the biomembrane on filler fully, reaches under conditions of blower fan 30 oxygen supply
To the rapid Degradation of Organic substance.Biological Contact Oxidation Process be a kind of between activated sludge process and biofilter it
Between bio membrane process, be characterized in arranging filler in pond, aeration at the bottom of pond carries out oxygenation to sewage, and makes
In cell body, sewage is in flow regime, to ensure that sewage is fully contacted with the filler in sewage, it is to avoid catalytic oxidation
Pond 10 exists sewage and contacts the defect of inequality with filler.Institute of Micro-biology is aerobic to be supplied by blast aeration, biological
After film grows to certain thickness, the microbes of filler wall carries out anaerobic metabolism because of anoxia, the gas of generation and
The souring that aeration is formed can cause biomembranous coming off, and promotes the growth of neoplasm film, now, comes off
Biomembrane will be flowed in sedimentation tank 18 by the overfall 15 of contact-oxidation pool with water outlet.
It is provided with reflux pump 20 and sludge pump 22 in described sedimentation tank 18, contact-oxidation pool 10 water outlet contains
Having a large amount of activated sludge, these mud are flowed in sedimentation tank 18 along with sewage, have under the effect of swash plate 19
The mud having good settling property can be good at carrying out mud-water separation, and isolated water up to standard is by opening draining
Electromagnetic valve 24 on mouth 23 is drained in river course 29 by drain pipe 25.In order to micro-in keeping contact-oxidation pool 10
Stable and the sludge aging impact on system of Biomass, a part of mud drains into contact oxygen by reflux pump 20
Changing in pond 10, another part drains in sludge-tank 27 by sludge pump 22, when concentrating full dirt in sludge-tank 27
During mud, mud can be discharged by sludge-tank manhole 28 by external device.
Described anaerobic pond manhole 9, contact-oxidation pool manhole 16, sedimentation tank manhole 26, sludge-tank manhole
28 are easy for staff enters each pond and safeguards equipment and keep in repair.
Described canyon 17 is internal has electric control gear, described electric control gear divide manual operation and are automatically brought into operation
Two parts.
With a certain engineering waste water control as background, the present invention is to the engineering index before and after sewage disposal such as
Under:
(1) influent CODcrMean concentration is 300mg/l, water outlet COD after processcrMean concentration 60mg/l
(standard≤100mg/l), CODcrAverage removal rate is 80%.
(2) water inlet BOD5Mean concentration is 200mg/l, water outlet BOD after process5Mean concentration is 15mg/l
(standard≤20mg/l), BOD5Average removal rate is 95%.
(3) water inlet NH3-N mean concentration is 30mg/l, water outlet NH after process3-N mean concentration is 10
Mg/l (standard≤15mg/l), NH3-N average removal rate is 75%.
(4) other in water outlet is about index, all can reach GB8978-1996 such as SS, PH etc. " comprehensive
Sewage drainage standard " in primary standard.
Claims (4)
- The most large-scale integrated sewage treating apparatus, including grid, regulating reservoir, anaerobic pond, contact-oxidation pool, sedimentation tank, Sludge-tank, fan house, canyon, it is characterised in that: described grids top is connected with sewage pipe, described tune Joint pond is wrapped in grid, and described liquid-level floater is positioned at inside regulating reservoir, and described elevator pump is positioned at bottom regulating reservoir, Described water pipe one end is connected with regulating reservoir, and the other end is connected with anaerobic pond, and described anaerobic pond is internal arranges that elasticity is filled out Material, described anaerobic pond manhole is positioned at anaerobic pond top, and described anaerobic pond overfall is positioned at anaerobic pond upper side even Lead to contact-oxidation pool, described contact-oxidation pool lower disposed gas distribution pipe, described gas distribution pipe is arranged rotary mixing type exposes Gas device, described gas distribution pipe is connected with the blower fan within fan house by airduct, and described contact-oxidation pool is internal to be arranged Elastic filler, described contact-oxidation pool manhole is positioned at contact-oxidation pool top, described contact-oxidation pool overfall position Connecting sedimentation tank in contact-oxidation pool upper side, swash plate, described sedimentation tank people are arranged in described sedimentation tank top Hole is positioned at sedimentation tank top, and described discharge outlet is positioned at sedimentation tank upper side and is communicated to river course by drain pipe, institute State and bottom sedimentation tank, arrange that reflux pump and sludge pump, described reflux pump are connected with contact-oxidation pool by sludge pipe, Described sludge pump is connected with sludge-tank by sludge pipe, described sludge-tank top layout sludge-tank manhole, described in set Standby room by circuit and the liquid-level floater in regulating reservoir and elevator pump, the reflux pump detested in sedimentation tank and sludge pump, Blower fan in fan house connects.
- The most large-scale integrated sewage treating apparatus, it is characterised in that: described regulating reservoir, detest Oxygen pond, contact-oxidation pool, sedimentation tank, sludge-tank, fan house, all of wall surface of canyon are coated with anticorrosion Material.
- The most large-scale integrated sewage treating apparatus, it is characterised in that: described anaerobic pond overflow The most significant end of mouth is less than the least significant end of contact-oxidation pool overfall.
- The sewage treatment process that the most large-scale integrated sewage treating apparatus is carried out, its feature It is: sewage, is entered in regulating reservoir by dispatch to grid by sewage pipe after the filtration of grid； When regulating reservoir liquid level reaches the high level of liquid-level floater setting, elevator pump starts automatically, and sewage is delivered to anaerobic pond In, when liquid level drops to the low liquid level of liquid-level floater setting, elevator pump is automatically stopped；When the boosted pumping of sewage To anaerobic pond, anaerobe, with elastic filler as carrier, carries out anaerobic biodegradation；Sewage is through anaerobic pond Overfall is flowed in contact-oxidation pool, and in sewage, major part Organic substance is degraded at this and purifies；Degraded and Sewage after purification and mud mixed liquid are flowed in sedimentation tank through contact-oxidation pool overfall, precipitate through sedimentation tank After, sewage up to standard is discharged in river course by drain pipe, and a mud part drains into contact oxygen by reflux pump Changing in pond, another part is drained in sludge-tank by sludge pump；When concentrating full mud in sludge-tank, can borrow Help external device to pass through sludge-tank manhole to be discharged by mud.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610624436.7A CN106007267A (en) | 2016-08-01 | 2016-08-01 | Large integrated sewage treatment device and sewage treatment technology |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610624436.7A CN106007267A (en) | 2016-08-01 | 2016-08-01 | Large integrated sewage treatment device and sewage treatment technology |
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| Publication Number | Publication Date |
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| CN106007267A true CN106007267A (en) | 2016-10-12 |
Family
ID=57133826
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610624436.7A Pending CN106007267A (en) | 2016-08-01 | 2016-08-01 | Large integrated sewage treatment device and sewage treatment technology |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107265758A (en) * | 2017-06-20 | 2017-10-20 | 深圳市天云环境工程有限公司 | The free of contamination comprehensive sewage treatment system of high efficiency smart |
| CN107698105A (en) * | 2017-11-10 | 2018-02-16 | 中冶华天工程技术有限公司 | A kind of city river rainwater discharge outlet pretreatment unit |
| CN110054301A (en) * | 2019-04-19 | 2019-07-26 | 江苏大学 | A kind of Drain contamination for river channel mouth sewage in-situ processing unit and processing method |
| CN110482798A (en) * | 2019-09-09 | 2019-11-22 | 扬州绿都环境工程设备有限公司 | A kind of intelligent integral sewage disposal device and technique |
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2016
- 2016-08-01 CN CN201610624436.7A patent/CN106007267A/en active Pending
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102897978A (en) * | 2012-10-17 | 2013-01-30 | 常州大学 | Taihu Lake region village sewage treatment and Duantou creek water environment repair method |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN107265758A (en) * | 2017-06-20 | 2017-10-20 | 深圳市天云环境工程有限公司 | The free of contamination comprehensive sewage treatment system of high efficiency smart |
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| CN107698105B (en) * | 2017-11-10 | 2024-04-16 | 中冶华天工程技术有限公司 | A pretreatment device for rainwater discharge outlet of urban river |
| CN110054301A (en) * | 2019-04-19 | 2019-07-26 | 江苏大学 | A kind of Drain contamination for river channel mouth sewage in-situ processing unit and processing method |
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Application publication date: 20161012 |