CN1821121A - Waste water treating process of circulation sequence batched active sludge and its active sludge reactor - Google Patents
Waste water treating process of circulation sequence batched active sludge and its active sludge reactor Download PDFInfo
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- CN1821121A CN1821121A CNA2006100185022A CN200610018502A CN1821121A CN 1821121 A CN1821121 A CN 1821121A CN A2006100185022 A CNA2006100185022 A CN A2006100185022A CN 200610018502 A CN200610018502 A CN 200610018502A CN 1821121 A CN1821121 A CN 1821121A
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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Abstract
The present invention discloses circular sequential batch active sludge process for treating waste water and its active sludge reactor. The reactor consists of two main reactor tanks and two auxiliary reactor tanks connected through passage or control valve to form a closed ring. Each of the main reactor tanks is provided with aerator and water inlet in the upstream tank wall; and each of the auxiliary reactor tanks is provided with stirrer, residual sludge pump, water inlet in the upstream tank wall and water drainer in the downstream tank wall. The present invention completes the circular plug-flow waste water treatment in the closed ring space comprising two main reactor tanks and two auxiliary reactor tanks, and makes the reactor tanks in anoxia, anaerobic, aerobic and deposit steps successively, so as to eliminate nitrogen and phosphate, degrade organic matter and separate solid from liquid. The present invention has the advantages of high treating effect, flexible management and low running cost.
Description
Technical field
The present invention relates to adopt the technology and the device thereof of activated sludge process degradation of sewage, refer to a kind of waste water treating process of circulation sequence batched active sludge and activated sludge reactor thereof particularly.
Background technology
The conventional activated sludge method is to use more general sewage disposal technology at present, it utilizes microorganism at first organism to be changed into carbonic acid gas, water and microbial cells, after the reaction microorganism is preserved, from system, remove newly-increased microorganism at reasonable time by getting rid of excess sludge, reach the purpose of pollution degradation load.Activated sludge process sewage disposal technology commonly used has the process forms such as combination of Continuous Flow, sequence batch (and Continuous Flow and sequence batch (.
Continuous flow process is changed this process of carrying out by the each processing unit spatial, and sewage at first enters the aerated reaction pond, enters settling tank then mixed solution is precipitated, and effluxes with supernatant liquor after microorganism separates.Sequence batch (technology then is that the alternately conversion by in time realizes this process, it concentrates on the function in aerated reaction pond and the heavy pond of secondary in the pond on flow process, the functions such as the adjusting of row water quality and quantity, microbiological deterioration organism and solid-liquid separation of holding concurrently.In recent years, along with going deep into and development of technology of research, the combination process of some Continuous Flow and sequence batch (has also obtained application.
Classical sequencing batch active sludge (SBR technology) is compared with traditional Continuous Flow activated sludge process, have reaction efficiency height, denitrogenation dephosphorizing, prevent sludge bulking, omit secondary sedimentation basins, do not need advantage such as mud backflow, but also exist the water of to be back to back, pond to hold simultaneously and defective such as plant factor is low and varying head draining, head loss be big.At present, SBR technology has obtained great development with its unique advantage, engineering technical personnel have developed the technologies such as ICEAS, CASS, IDEA and DAT-IAT of continuous water inlet, liquid level variable water outlet successively, and can intake continuously and sequence batch (s such as UNITANK, the LUCAS of permanent liquid level water outlet and MSBR improve technology.
These improved SBR technologies are solving classical SBR technology continuously in the shortcoming such as water-in and water-out, improve volume and plant factor, strengthened the effect of partially disposed, but also caused shortcomings such as sedimentation effect is relatively poor, complicated, the single pond of operational management control load is unbalanced.Denitrogenation dephosphorizing effect as ICEAS, DAT-IAT, LUCAS and UNITANK is relatively poor; CASS has good denitrogenation dephosphorizing function, but can not continuous effluent; MSBR has good denitrogenation dephosphorizing effect for combination seven pool structures, but equipment and Controlling System complexity, cost are higher.In a word, these improved SBR technologies have all solved the problem that classical SBR technology exists to some extent, but the advantage of the classical SBR technology that also more or less weakened, cause existing in the practical application many weak points, the stability of process system operation and the effect of sewage disposal all are subjected to influence in various degree, and these problems await improving with perfect.
Summary of the invention
The objective of the invention is at the deficiency in existing SBR and the improved technology thereof, aim to provide the waste water treating process of circulation sequence batched active sludge that a kind of treatment effect is good, management is flexible, working cost is low, and the circulation batch type activated sludge reactor that is used for this technology.
For achieving the above object, the waste water treating process of circulation sequence batched active sludge that the present invention is designed comprises the four-stage that circular flow is disposed of sewage, wherein:
Fs comprises following process:
(1) opens the water-in that reaction tank is assisted in the first main reaction pond and first, sewage is imported in it, and the aerating apparatus in the first main reaction pond stops aeration, make sewage be in anoxic condition, this moment, microorganism was a carrier with the organism in the water inlet, by the denitrification realization denitrogenation of amphimicrobe.
The sewage mixed solution in (2) first main reaction ponds enters the first auxilliary reaction tank by a communication channel, and the whipping appts in the first auxilliary reaction tank is opened and is stirred, make sewage be in anaerobic state, the microorganism that the previous cycle of operation precipitates is a carrier with the organism in the water inlet, the phosphorus in the excessive release mud.
(3) close the water-in that reaction tank is assisted in the second main reaction pond and second, open the control sluice between the first auxilliary reaction tank and the second main reaction pond, make the sewage mixed solution enter the second main reaction pond, and the aerating apparatus blast aeration in the second main reaction pond, make sewage be in oxygen condition, microorganism carries out organic matter degradation, nitration reaction and excessive adsorption phosphorus.
The sewage mixed solution in (4) second main reaction ponds enters as second of settling tank by another communication channel and assists reaction tank, close the control sluice between the second auxilliary reaction tank and the first main reaction pond, and the whipping appts in the second auxilliary reaction tank stops to stir, mud-water separation in the sewage, supernatant liquor is discharged by water-freeing arrangement, and excess sludge is then got rid of by residual sludge pump; The time length of fs is 120～180 minutes.
Subordinate phase is a transitory stage, closes the water-in of the first main reaction pond and the first auxilliary reaction tank, closes the control sluice between the first auxilliary reaction tank and the second main reaction pond; Open the water-in in the second main reaction pond, open the control sluice between the second auxilliary reaction tank and the first main reaction pond, and the aerating apparatus blast aeration in the first main reaction pond, sewage change by the water inlet of the second main reaction pond, and the second auxilliary reaction tank still is in quiescent setting and goes out water state; The time length of subordinate phase is 30～60 minutes, makes that the mud that is about to as in the first auxilliary reaction tank of settling tank is settled down.
The function of phase III with the fs is identical, just on operation scheme, the second main reaction pond has replaced the first main reaction pond, and the second auxilliary reaction tank has replaced the first auxilliary reaction tank, sewage is entered by the second main reaction pond and the second auxilliary reaction tank, and clear water flows out from the first auxilliary reaction tank.
The quadravalence section is identical with the function of subordinate phase, just on operation scheme, from the water inlet of the first main reaction pond, first assists the reaction tank water outlet, make the mud that is about to as in the second auxilliary reaction tank of settling tank be able to sedimentation, guarantee that working order comes back to the fs; Go round and begin again thus, constantly circulation, thus make sewage purification.
For realizing the custom-designed circulation batch type activated sludge reactor of above-mentioned sewage treatment process, comprise four sewage reaction tanks, described four sewage reaction tanks are in series by the first main reaction pond, the first auxilliary reaction tank, the second main reaction pond and the second auxilliary reaction tank ring seal successively.Wherein: be provided with a communication channel between the first main reaction pond and the first auxilliary reaction tank, be provided with a control sluice between the first auxilliary reaction tank and the second main reaction pond, be provided with another communication channel between the second main reaction pond and the second auxilliary reaction tank, be provided with another control sluice between the second auxilliary reaction tank and the first main reaction pond, constitute the circulation passage that the sewage plug-flow is handled thus.And:
Be respectively arranged with aerating apparatus in the first and second main reaction ponds, be furnished with main reaction pond water-in respectively on the circulating water flow upstream pool wall in the first and second main reaction ponds; Be respectively arranged with whipping appts and residual sludge pump in the first and second auxilliary reaction tanks, be furnished with auxilliary reaction tank water-in on the circulating water flow upstream pool wall of the first and second auxilliary reaction tanks respectively, be furnished with water-freeing arrangement respectively on the circulating water flow downstream pool wall of the first and second auxilliary reaction tanks.
Conclusion is got up, and sewage treatment process of the present invention and circulation batch type activated sludge reactor thereof have the characteristics of following six aspects:
1) on the pond of reaction tank type is arranged, function with multipoint water feeding and multiple spot water outlet, and the mutual series circulation of each unit cells both can be according to the technology mode operations of Continuous Flow, can switch to the technology mode operation of sequence batch (again, simultaneously can also the cyclical operation operation.
2) in the equipment configuration of each unit cells, can be according to the reaction mechanism of microorganism, the different characteristics of solid-liquid separation, according to functional requirement different water-ins, aerating apparatus, whipping appts, precipitated outlet water device are set, satisfy the requirement that switch in art breading unit time and space.
3) in each unit cells, can circulate the operation of operating device by time-program(me), space, make each unit cells be in anoxic, anaerobism, aerobic and precipitation operation respectively, thereby make the corresponding function of whole reactor with denitrogenation dephosphorizing, degradation of organic substances, solid-liquid separation.
4) can adopt be applicable to satisfy aeration, the precipitation working condition requirement permanent liquid level, exempt to pollute water-freeing arrangement.
5) in the whole service cycle of waste water treating process of circulation sequence batched active sludge, the Inlet and outlet water continuously-running, match with actual flooded condition, do not need to take measures in addition or setting device is set, because this technology is uninterrupted circular flow, can overcome the uneven situation of sludge concentration simultaneously.
6) each unit cells function division is clear and definite, and plant factor has been improved based on the microorganism aeration in the main reaction pond; Auxilliary reaction tank has utilized biology to staticly settle the characteristics good with the advection sedimentation effect in the combination of pond type, can guarantee effluent quality.
In sum, compare, the invention has the advantages that with existing SBR technology:
One, good sewage processing effect.Circulation batch type activated sludge reactor of the present invention combines the advantage of Continuous Flow and sequence batch (sludge reaction device, present ecological diversity in the microbial reaction stage, anaerobism, anoxic and various states such as aerobic appear, the efficient of dephosphorization denitrogenation, and organic matter removal effectively height.And at the microorganism precipitate phase, staticly settling is that ideal precipitates, and sedimentation function is good, and effluent quality is excellent.
Its two, construction investment is economized.Waste water treating process of circulation sequence batched active sludge of the present invention is the high integrated sewage water New Process for Treatment of intensification degree, it is not provided with preliminary sedimentation tank and second pond, operation continuously under permanent water level, and adopt single pond many lattice mode, need not to be interrupted flow, saved many pool process required more multi-link pipe, pump, valve and reflux.From the reliability of system, civilwork engineering quantity, total installation of generating capacity, energy-conservation, reduce running cost and many-side such as save the area, have remarkable advantages than traditional sewage treatment process.
Its three, working cost is low.Waste water treating process of circulation sequence batched active sludge of the present invention adopts the operation of circulation plug-flow, and the water quality load is ideal plug-flow state, dynamic efficiency height.Its activated sludge reactor does not need mud to reflux and mixed-liquor return, and it adopts permanent liquid level water discharge technology to avoid the head loss of liquid level variable simultaneously, has saved working cost greatly than traditional sewage treatment process.
Its four, small accommodation area.Circulation batch type activated sludge reactor of the present invention can be compact more on structural arrangement, as whole employing rectangle reaction tank combinations, compare with traditional circular reaction tank, the rectangle reaction tank can shared pool wall, thereby reduce floor space and concrete amount, and system's dark scope in selectable pond is bigger, can reach 3.50～8.00m, fully saves the area.
Its five, capacity of resisting impact load is strong.Circulation batch type activated sludge reactor of the present invention divides multipoint water feeding, has effectively improved the ability that water impact load and organism impact load bear in system.The sludge loading and the volumetric loading of system improve greatly, in anaerobism, anoxic and various states such as aerobic, have improved the processing efficiency of used water difficult to degradate.
Its six, processing unit is simple, controls flexible automatically.
Therefore, Processes and apparatus of the present invention is very simple and practical, adopts permanent liquid level discharging device, and the hydrophone power consumption is big, mechanical part is many, the deficiency of life-span weak point to have avoided traditional straining.Can combine complicated manual operation and computer, software, plant and instrument by existing automatic control system, finish the entire sewage treatment process automatically, create the optimum environment that satisfies microorganism existence.
Description of drawings
Accompanying drawing is that a kind of two dimensional structure of circulation batch type activated sludge reactor is arranged synoptic diagram.
Embodiment
Below in conjunction with the drawings and specific embodiments waste water treating process of circulation sequence batched active sludge of the present invention and activated sludge reactor thereof are described in further detail:
Circulation batch type activated sludge reactor of the present invention shown in the figure has four sewage reaction tanks that structure is rectangular.Four rectangle sewage reaction tanks are divided into the first main reaction pond, 1, the first auxilliary reaction tank 2, the second main reaction pond 3 and the second auxilliary reaction tank 4, wherein: the dimensional parameters in the first and second main reaction ponds 1,3 is identical, they are arranged in juxtaposition together, and pool wall of shared intermediary; The dimensional parameters of the first and second auxilliary reaction tanks 2,4 is identical, they are arranged in the both sides in the first and second main reaction ponds 1,3, and their pool wall is the both sides pool wall in the shared first and second main reaction ponds 1,3 simultaneously, thereby makes four reaction tanks also rectangular structure on integral planar is arranged.
Shared pool wall between the first main reaction pond 1 and the first auxilliary reaction tank 2 is provided with a communication channel 16, shared pool wall between the first auxilliary reaction tank 2 and the second main reaction pond 3 is provided with an electronic control sluice 11, the shared pool wall that shared pool wall between the second main reaction pond 3 and the second auxilliary reaction tank 4 is provided with between another communication channel 17, the second auxilliary reaction tanks 4 and the first main reaction pond 1 is provided with another electronic control sluice 12.Above-mentioned communication channel 16,17 is a structure open in usual, makes the first main reaction pond 1 and the first auxilliary reaction tank 2, the second main reaction pond 3 and the second auxilliary reaction tank 4 always be in connected state; 11,12 processing requirements according to sewage disposal of above-mentioned electronic control sluice open and close, thereby control the break-make between the first auxilliary reaction tank 2 and the second main reaction pond, 3, the second auxilliary reaction tank 4 and the first main reaction pond 1.Like this, four sewage reaction tank ring seal series connection successively constitute the circulation passage that the sewage plug-flow is handled.
In the first and second main reaction ponds 1,3, be respectively arranged with aerating apparatus 13, on the circulating water flow upstream pool wall in the first and second main reaction ponds 1,3, be furnished with main reaction pond water-in 5,7 respectively.In the first and second auxilliary reaction tanks 2,4, be respectively arranged with whipping appts 14 and residual sludge pump 15, on the circulating water flow upstream pool wall of the first and second auxilliary reaction tanks 2,4, be furnished with auxilliary reaction tank water-in 6,8 respectively, on the circulating water flow downstream pool wall of the first and second auxilliary reaction tanks 2,4, be furnished with water-freeing arrangement 9,10 respectively.Above-mentioned various device is equipment well-known to those skilled in the art, seldom gives unnecessary details in this.
Waste water treating process of circulation sequence batched active sludge of the present invention moves by loop cycle.In with one-period, operational process is divided into four-stage, each reaction tank adopts different drive manners in the different time periods, to finish different processing intents, guarantees the effect of final sewage disposal.With a complete cycle be example:
Fs comprises following process:
The water-in 5,6 of (1) the first main reaction pond 1 and the first auxilliary reaction tank 2 is in opened condition, and sewage is imported in the first main reaction pond 1 and the first auxilliary reaction tank 2.And, open the electronic control sluice 11 between the first auxilliary reaction tank 2 and the second main reaction pond 3, close the electronic control sluice 12 between the second auxilliary reaction tank 4 and the first main reaction pond 1.Simultaneously, the aerating apparatus 13 in the first main reaction pond 1 stops aeration, makes sewage be in anoxic condition, and microorganism is a carrier with the organism in the water inlet, by the denitrification realization denitrogenation of amphimicrobe.
Sewage mixed solution in (2) the first main reaction ponds 1 enters the first auxilliary reaction tank 2 by the communication channel on the pool wall 16, and the whipping appts 14 in the first auxilliary reaction tank 2 is opened and is stirred, make sewage be in anaerobic state, the microorganism that the previous cycle of operation precipitates is a carrier with the organism in the water inlet, the phosphorus in the excessive release mud.
The water-in 7,8 of (3) the second main reaction ponds 3 and the second auxilliary reaction tank 4 is in closing condition, and the sewage mixed solution in the first auxilliary reaction tank 2 enters the second main reaction pond 3 by the electronic control sluice 11 on the pool wall.Simultaneously, aerating apparatus 13 blast aerations in the second main reaction pond 3 make sewage be in oxygen condition, and microorganism carries out organic matter degradation, nitration reaction and excessive adsorption phosphorus.
Sewage mixed solution in (4) the second main reaction ponds 3 enters as second of settling tank by the communication channel on the pool wall 17 and assists reaction tank 4, the electronic control sluice 12 that assist between the reaction tank 4 and the first main reaction pond 1 this moment second still is in closing condition, whipping appts 14 in the second auxilliary reaction tank 4 stops to stir, mud-water separation in the sewage, supernatant liquor is discharged by water-freeing arrangement 10, and excess sludge is then got rid of by residual sludge pump 15.The time length of whole fs generally was controlled at 120～180 minutes.
Subordinate phase is a transitory stage, close the water-in 5,6 of the first main reaction pond 1 and the first auxilliary reaction tank 2 this moment, close the electronic control sluice 11 between the first auxilliary reaction tank 2 and the second main reaction pond 3, open the water-in 7 in the second main reaction pond 3, open the electronic control sluice 12 between the second auxilliary reaction tank 4 and the first main reaction pond 1.Simultaneously, aerating apparatus 13 blast aerations in the first main reaction pond 1, sewage changes by 3 water inlets of the second main reaction pond, and the second auxilliary reaction tank 4 still is in quiescent setting and goes out water state.The time length of whole subordinate phase generally was controlled at 30～60 minutes, made that the mud that is about to as in the first auxilliary reaction tank 2 of settling tank is settled down.
The function of phase III with the fs is identical, just on operation scheme, the second main reaction pond 3 has replaced the first main reaction pond, 1, the second auxilliary reaction tank 4 and has replaced the first auxilliary reaction tank 2, sewage is entered by the second main reaction pond 3 and the second auxilliary reaction tank 4, and clear water flows out from the first auxilliary reaction tank 2.The time length of phase III is identical with the fs.
The quadravalence section is consistent with the function of subordinate phase, be similarly a transitory stage, just on operation scheme, change into from 1 water inlet of the first main reaction pond, first auxilliary reaction tank 2 water outlets, make the mud that is about to as in the second auxilliary reaction tank 4 of settling tank be able to sedimentation, guarantee that working order comes back to the fs.Go round and begin again like this, circular flow, thus reach the target of purifying waste water.
Claims (3)
1. a waste water treating process of circulation sequence batched active sludge comprises the four-stage that circular flow is disposed of sewage, wherein:
Fs comprises following process:
(1) opens the water-in that reaction tank is assisted in the first main reaction pond and first, sewage is imported in it, and the aerating apparatus in the first main reaction pond stops aeration, make sewage be in anoxic condition, this moment, microorganism was a carrier with the organism in the water inlet, by the denitrification realization denitrogenation of amphimicrobe;
The sewage mixed solution in (2) first main reaction ponds enters the first auxilliary reaction tank by a communication channel, and the whipping appts in the first auxilliary reaction tank is opened and is stirred, make sewage be in anaerobic state, the microorganism that the previous cycle of operation precipitates is a carrier with the organism in the water inlet, the phosphorus in the excessive release mud;
(3) close the water-in that reaction tank is assisted in the second main reaction pond and second, open the control sluice between the first auxilliary reaction tank and the second main reaction pond, make the sewage mixed solution enter the second main reaction pond, and the aerating apparatus blast aeration in the second main reaction pond, make sewage be in oxygen condition, microorganism carries out organic matter degradation, nitration reaction and excessive adsorption phosphorus;
The sewage mixed solution in (4) second main reaction ponds enters as second of settling tank by another communication channel and assists reaction tank, close the control sluice between the second auxilliary reaction tank and the first main reaction pond, and the whipping appts in the second auxilliary reaction tank stops to stir, mud-water separation in the sewage, supernatant liquor is discharged by water-freeing arrangement, and excess sludge is then got rid of by residual sludge pump; The time length of fs is 120～180 minutes;
Subordinate phase is a transitory stage, closes the water-in of the first main reaction pond and the first auxilliary reaction tank, closes the control sluice between the first auxilliary reaction tank and the second main reaction pond; Open the water-in in the second main reaction pond, open the control sluice between the second auxilliary reaction tank and the first main reaction pond, and the aerating apparatus blast aeration in the first main reaction pond, sewage change by the water inlet of the second main reaction pond, and the second auxilliary reaction tank still is in quiescent setting and goes out water state; The time length of subordinate phase is 30～60 minutes, makes that the mud that is about to as in the first auxilliary reaction tank of settling tank is settled down;
The function of phase III with the fs is identical, just on operation scheme, the second main reaction pond has replaced the first main reaction pond, and the second auxilliary reaction tank has replaced the first auxilliary reaction tank, sewage is entered by the second main reaction pond and the second auxilliary reaction tank, and clear water flows out from the first auxilliary reaction tank;
The quadravalence section is identical with the function of subordinate phase, just on operation scheme, from the water inlet of the first main reaction pond, first assists the reaction tank water outlet, make the mud that is about to as in the second auxilliary reaction tank of settling tank be able to sedimentation, guarantee that working order comes back to the fs; Go round and begin again thus, constantly circulation, thus make sewage purification.
2. the circulation batch type activated sludge reactor that the described sewage treatment process of claim 1 is used comprises four sewage reaction tanks, it is characterized in that:
Described four sewage reaction tanks are by the first main reaction pond (1), the first auxilliary reaction tank (2), the second main reaction pond (3) and the second auxilliary reaction tank (4) ring seal successively are in series, wherein: be provided with a communication channel (16) between the first main reaction pond (1) and the first auxilliary reaction tank (2), be provided with a control sluice (11) between the first auxilliary reaction tank (2) and the second main reaction pond (3), be provided with another communication channel (17) between the second main reaction pond (3) and the second auxilliary reaction tank (4), be provided with another control sluice (12) between the second auxilliary reaction tank (4) and the first main reaction pond (1), constitute the circulation passage that the sewage plug-flow is handled thus;
Be respectively arranged with aerating apparatus (13) in described first, second main reaction pond (1,3), be furnished with main reaction pond water-in (5,7) on the circulating water flow upstream pool wall of first, second main reaction pond (1,3) respectively;
Be respectively arranged with whipping appts (14) and residual sludge pump (15) in described first, second auxilliary reaction tank (2,4), be furnished with auxilliary reaction tank water-in (6,8) on the circulating water flow upstream pool wall of first, second auxilliary reaction tank (2,4) respectively, be furnished with water-freeing arrangement (9,10) on the circulating water flow downstream pool wall of first, second auxilliary reaction tank (2,4) respectively.
3. circulation batch type activated sludge reactor according to claim 2, it is characterized in that: the said first main reaction pond (1), the first auxilliary reaction tank (2), the second main reaction pond (3) and the second auxilliary all rectangular structure of reaction tank (4), wherein: first, the second main reaction pond (1,3) dimensional parameters is identical, they are arranged in juxtaposition together, and pool wall of shared intermediary, first, the second auxilliary reaction tank (2,4) dimensional parameters is identical, they are arranged in first, the second main reaction pond (1,3) both sides, and their a pool wall while shared first, the second main reaction pond (1,3) both sides pool wall, thus make the also rectangular on the whole structure of four reaction tanks; Control sluice (11,12) between communication channel (16,17) between said first, second main reaction pond (1,3) and first, second the auxilliary reaction tank (2,4) and first, second auxilliary reaction tank (2,4) and second, the first main reaction pond (3,1) all is arranged on their the shared pool wall.
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Cited By (8)
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| CN100460341C (en) * | 2007-06-21 | 2009-02-11 | 中国海洋大学 | Biological sewage-treating process |
| CN102502963A (en) * | 2011-11-04 | 2012-06-20 | 浦华环保有限公司 | Multi-mode sequencing batch active sludge sewage treatment method and system |
| CN101570379B (en) * | 2009-06-08 | 2012-08-08 | 陈明 | Communicated adjustment type sewage treatment equipment |
| CN102933506A (en) * | 2010-01-28 | 2013-02-13 | K·英格尔 | Method and device for biological wastewater purification |
| CN104291530A (en) * | 2014-10-17 | 2015-01-21 | 中山环保产业股份有限公司 | Sequencing batch biochemical sewage treatment device and sedimentation-drainage method thereof |
| CN104341076A (en) * | 2013-08-02 | 2015-02-11 | 湖北盘古环保工程技术有限公司 | Continuous biochemical reaction and intermittent static precipitation integrated sewage treatment device |
| CN105540850A (en) * | 2016-02-29 | 2016-05-04 | 东南大学 | Nitrogen and phosphorus removal method adopting anoxic, anaerobic and aerobic circular alternation |
| CN105668940A (en) * | 2016-03-31 | 2016-06-15 | 武汉绿明利环能股份有限公司 | Ecological ICPS municipal domestic sewage treatment method |
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| NL1006753C2 (en) * | 1997-08-08 | 1999-02-09 | Waterleiding Friesland Nv | Method for decolorizing liquids, in particular groundwater, using a membrane filtration unit, device for use in such a method, as well as decolorized groundwater. |
| CN1509995A (en) * | 2002-12-25 | 2004-07-07 | 宜兴鹏鹞阳光环保有限公司 | Improved sewage secondary biochemical treating process and reactor |
| CN1242940C (en) * | 2003-11-04 | 2006-02-22 | 广州大学 | Method for treating urban sewage through denitrifying process for phophorous removal and defluorination |
| CN1544364A (en) * | 2003-11-17 | 2004-11-10 | 李迪田 | Propulsive and batched type activated sludge reaction process and device |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN100460341C (en) * | 2007-06-21 | 2009-02-11 | 中国海洋大学 | Biological sewage-treating process |
| CN101570379B (en) * | 2009-06-08 | 2012-08-08 | 陈明 | Communicated adjustment type sewage treatment equipment |
| CN102933506A (en) * | 2010-01-28 | 2013-02-13 | K·英格尔 | Method and device for biological wastewater purification |
| CN102502963A (en) * | 2011-11-04 | 2012-06-20 | 浦华环保有限公司 | Multi-mode sequencing batch active sludge sewage treatment method and system |
| CN102502963B (en) * | 2011-11-04 | 2013-07-10 | 浦华环保有限公司 | Multi-mode sequencing batch active sludge sewage treatment method and system |
| CN104341076A (en) * | 2013-08-02 | 2015-02-11 | 湖北盘古环保工程技术有限公司 | Continuous biochemical reaction and intermittent static precipitation integrated sewage treatment device |
| CN104291530A (en) * | 2014-10-17 | 2015-01-21 | 中山环保产业股份有限公司 | Sequencing batch biochemical sewage treatment device and sedimentation-drainage method thereof |
| CN104291530B (en) * | 2014-10-17 | 2016-05-04 | 中山环保产业股份有限公司 | A kind of method of batch-type biochemical sewage treatment device and sedimentation and drawing thereof |
| CN105540850A (en) * | 2016-02-29 | 2016-05-04 | 东南大学 | Nitrogen and phosphorus removal method adopting anoxic, anaerobic and aerobic circular alternation |
| CN105540850B (en) * | 2016-02-29 | 2017-12-26 | 东南大学 | Cycle alternation hypoxic/anaerobic/aerobic nitrogen removal phosphorus removing method |
| CN105668940A (en) * | 2016-03-31 | 2016-06-15 | 武汉绿明利环能股份有限公司 | Ecological ICPS municipal domestic sewage treatment method |
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| CN100369830C (en) | 2008-02-20 |
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