CN204661498U - Adopt pre-treatment and micro-aeration two benches formula less energy-consumption Sewage treatment systems - Google Patents
Adopt pre-treatment and micro-aeration two benches formula less energy-consumption Sewage treatment systems Download PDFInfo
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- CN204661498U CN204661498U CN201520250076.XU CN201520250076U CN204661498U CN 204661498 U CN204661498 U CN 204661498U CN 201520250076 U CN201520250076 U CN 201520250076U CN 204661498 U CN204661498 U CN 204661498U
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Abstract
Employing pre-treatment of the present utility model and micro-aeration two benches formula less energy-consumption Sewage treatment systems, comprise pretreatment pool, pre-treatment settling tank, denitrification tank, gas blower, controller and detector, sewage is aeration in pretreatment pool, and the organism in sewage and suspended substance are by sludge absorption; In pre-treatment settling tank, mud realizes sedimentation; Enter the sewage of denitrification tank, denitrogenation is carried out through the mode that micro-aeration runs or intermittent aeration runs, mineralized nitrogen is nitrite nitrogen by nitrite bacteria, and then ammonia nitrogen and nitrite nitrogen are together converted into nitrogen by anaerobic ammonia oxidizing bacteria, realize the removal of dissolubility pollutant in sewage.Sewage treatment systems of the present utility model, relies on the denitrogenation of anaerobic ammonia oxidizing bacteria, the nitrogen element overwhelming majority is converted into nitrogen, really have left water body and pollutent.In the sludge treatment stage, by anaerobically fermenting, organism is converted into the energy, considerable self electric quantity consumption can be brought for Sewage Plant, and keep the activity of denitrification microorganism.
Description
Technical field
The utility model relates to a kind of employing pre-treatment and micro-aeration two benches formula less energy-consumption Sewage treatment systems, in particular, particularly relate to and a kind ofly the sewage of the low ratio of carbon to ammonium of organics removal is carried out denitrogenation processing, by containing organic inorganic Sewage treatment systems of carrying out anaerobically fermenting.
Background technology
Generally present ammonia nitrogen concentration in China's town sewage too high, cause carbon-nitrogen ratio lower than 4 feature.Bio-denitrifying sewage process comprises ammonification, nitrification and denitrification three processes.Ammonification and nitrifying process need aeration to reach object organonitrogen and ammonia nitrogen being transformed completely nitre nitrogen, and energy consumption is huge.Denitrification process needs to provide abundant organism to make nitre nitrogen transformation in water body for nitrogen.And treating processes in the past, part nitrogen element absorbs ammonia nitrogen removal by the own growth demand of microorganism, in fact Sewage Plant part is not left, but be transferred in mud, and be released into again in Digestive system in sludge handling process, Digestive system foldback enters waste water processes, adds processing load.On the other hand, because in sewage, carbon-nitrogen ratio is lower, it is incomplete that common process often presents denitrification, is difficult to the nitrogen element in sewage to be removed completely, or thus adds the running cost that extra carbon source turn increases Sewage Plant.In addition, owing to needing sewage to experience different environment, sewage is constantly distributed and is refluxed in whole treatment scheme, and controlling factor is too much, and operating process is very complicated.
Summary of the invention
The utility model, in order to overcome the shortcoming of above-mentioned technical problem, provides a kind of employing pre-treatment and micro-aeration two benches formula less energy-consumption Sewage treatment systems.
Employing pre-treatment of the present utility model and micro-aeration two benches formula less energy-consumption Sewage treatment systems, its special feature is: comprise pretreatment pool, pre-treatment settling tank, denitrification tank, gas blower, controller and detector, the outlet of pretreatment pool communicates with the import of pre-treatment settling tank, and the water outlet of pre-treatment settling tank communicates with the import of denitrification tank; Gas blower realizes the aeration of pretreatment pool and denitrification tank, detector detects the water quality that the water quality and denitrification tank that are flowed to pre-treatment settling tank by pretreatment pool flow out, and controller controls the normal operation of whole Sewage treatment systems according to the detected result of detector to water quality;
Sewage is through the aeration effect of gas blower in pretreatment pool, and the organism in sewage and suspended substance are by sludge absorption; In pre-treatment settling tank, mud realizes sedimentation, and after mud and sewage are separated, sewage enters in denitrification tank through water outlet, and mud is returned in pretreatment pool through the sludge outlet of pre-treatment settling tank by foldback; Enter the sewage of denitrification tank, denitrogenation processing is carried out through the mode that micro-aeration runs or intermittent aeration runs, under the synergy of nitrite bacteria and anaerobic ammonia oxidizing bacteria, first the mineralized nitrogen in sewage is nitrite nitrogen by nitrite bacteria, and then ammonia nitrogen and nitrite nitrogen are together converted into nitrogen by anaerobic ammonia oxidizing bacteria, realize the removal of dissolubility pollutant in sewage.
Employing pre-treatment of the present utility model and micro-aeration two benches formula less energy-consumption Sewage treatment systems, the residence time of sewage in pretreatment pool, in pretreatment pool and pre-treatment settling tank, the mud of mud selected 1 ~ 5 day age between 30min ~ 120min; Be provided with whipping appts in denitrification tank, the residence time of sewage in denitrification tank, in denitrification tank, the mud of mud selected 50 days to 120 days age between 6h ~ 24h.
Employing pre-treatment of the present utility model and micro-aeration two benches formula less energy-consumption Sewage treatment systems, comprise sludge digestion tank and denitrifying sludge storage pool, the import of sludge digestion tank communicates with the sludge outlet of pre-treatment settling tank, so that the mud that pre-treatment settling tank is discharged enters in sludge digestion tank; Mud adopts the mode of anaerobically fermenting to stablize in sludge digestion tank, and organic substance is converted into the biogas energy, and the mud in sludge digestion tank is as disposition of solid waste;
The liquid exit of sludge digestion tank communicates with the import of denitrifying sludge storage pool, so that the Digestive system containing ammonia nitrogen in high density enters in denitrifying sludge storage pool; The sludge outlet of denitrification tank communicates with the mud import of denitrifying sludge storage pool, so that the mud in denitrification tank enters in denitrifying sludge storage pool.
Employing pre-treatment of the present utility model and micro-aeration two benches formula less energy-consumption Sewage treatment systems, the treatment time of mud in sludge digestion tank is 15 days to 100 days, be provided with whipping appts in denitrifying sludge storage pool, the sewage produced when denitrifying sludge storage pool stops stirring enters in pretreatment pool through water outlet; The mud that denitrifying sludge storage pool produces is used as the operation maintaining Sewage Plant self, also can be used as the inoculation denitrifying sludge of other Sewage Plant simultaneously.
Employing pre-treatment of the present utility model and micro-aeration two benches formula less energy-consumption Sewage treatment systems, the front end of described pretreatment pool is also provided with the pretreatment pool regulated water quality and the water yield for the treatment of sewage; Be provided with the filtering film component of most of sludge retention in denitrification tank in denitrification tank, realize being separated completely of water body and mud, also ensure that the enrichment of denitrifier.
Employing pre-treatment of the present utility model and micro-aeration two benches formula less energy-consumption Sewage treatment systems, the carbon-nitrogen ratio being flowed into denitrification tank sewage by pre-treatment settling tank is less than 2; If denitrification tank adopts micro-Air Exposure, the dissolved oxygen in sewage controls below 0.5, if denitrification tank adopts the method for intermittent aeration, wherein aeration phase dissolved oxygen maintains less than 2.
The beneficial effects of the utility model are: Sewage treatment systems of the present utility model, according to the feature that Ammonia Nitrogen in Sewage levels is too high, first under the condition of aeration, pre-treatment is carried out to sewage, by the absorption of microorganism to dirty Organic substance in water and suspended substance, the sewage after sedimentation is made to have lower carbon-nitrogen ratio.Sewage after sedimentation is at nitrogen removal stage, anaerobic ammonia oxidizing bacteria is utilized to have certain oxygen resistence, be able to carry out nitrosification and denitrification process in a pond, first mineralized nitrogen in sewage is nitrite nitrogen by nitrite bacteria, and then ammonia nitrogen and nitrite nitrogen are together converted into nitrogen by anaerobic ammonia oxidizing bacteria, realize the denitrogenation processing of sewage.
In sludge handling process, the mud organic substance content utilizing pretreatment stage to discharge is high, and the mud that nitrogen removal stage is discharged is rich in the feature of anaerobic ammonia oxidizing bacteria, anaerobically fermenting is carried out to the mud that pretreatment stage is got rid of, not only can produce the biogas energy of supplementary sewage work energy consumption, but also avoiding the energy expenditure in the past utilizing the growth of mushroom to bring to eliminate dirty Organic substance in water, energy-saving effect is remarkable; Mixed with the Digestive system produced in anaerobic fermentation process by mud denitrogenation produced, Asia utilizes nitrobacteria to be nitrite nitrogen by mineralized nitrogen, for anaerobic ammonia oxidizing bacteria provides matrix, to keep it active.
Sewage treatment systems of the present utility model, nitrogen removal stage, the main denitrogenation relying on anaerobic ammonia oxidizing bacteria, the nitrogen element overwhelming majority of nitrogen removal stage is converted into nitrogen, really have left water body and pollutent.Because the doubling time of microorganism is long, sludge yield is minimum, microbiologically stabilised, is mainly stored, stop in the past in sewage treatment process sludge-digestion liquid return sewage treatment process, increase the shortcoming of processing load.Organic pollutant in water inlet entered in the sludge treatment stage, and was converted into the energy, can bring considerable self electric quantity consumption for Sewage Plant.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of employing pre-treatment of the present utility model and micro-aeration two benches formula less energy-consumption Sewage treatment systems.
In figure: 1 equalizing tank, 2 pretreatment pools, 3 pre-treatment settling tanks, 4 denitrification tanks, 5 filtering film components, 6 sludge digestion tanks, 7 denitrifying sludge storage pools, 8 gas blowers, 9 controllers, 10 detectors.
Embodiment
Below in conjunction with accompanying drawing and embodiment, the utility model is described in further detail.
As shown in Figure 1, give the schematic diagram of employing pre-treatment of the present utility model and micro-aeration two benches formula less energy-consumption Sewage treatment systems, it comprises equalizing tank 1, pretreatment pool 2, pre-treatment settling tank 3, denitrification tank 4, filtering film component 5, sludge digestion tank 6, denitrifying sludge storage pool 7, gas blower 8, controller 9 and detector 10, shown equalizing tank 1 is positioned at the front end of pretreatment pool 2, first sanitary sewage enters in equalizing tank 1, equalizing tank 1 pair of water quality and the water yield regulate, reduce and misunderstand treatment scheme water quality, the fluctuation of the water yield, coordinate the constant of whole Sewage treatment systems flow.
The water outlet of pretreatment pool 2 communicates with the import of pre-treatment settling tank 3, and the water outlet of pre-treatment settling tank 6 communicates with denitrification tank 4, and the sludge outlet of pre-treatment settling tank 3 communicates with pretreatment pool 2 and sludge digestion tank 6.The sludge outlet of denitrification tank 4 communicates with denitrifying sludge storage pool 7, and the water outlet of sludge digestion tank 6 communicates with denitrifying sludge storage pool 7, so that the Digestive system produced enters in denitrifying sludge storage pool 7.Gas blower 8 is for carrying out aeration operation to pretreatment pool 2 and denitrification tank 4, the water quality of detector 10 pairs of pretreatment pool 2 effluent sewerages and the draining water quality of denitrification tank 4 detect, controller 9, according to the detection data of detector 10, controls the operation of whole Sewage treatment systems.
The sewage got rid of by equalizing tank 1 enters in pretreatment pool 2, because the sewage through regulating contains the extremely putrefactive pollutents such as a large amount of organism, in pretreatment pool 2, organic loading can be higher, should provide enough large aeration rate by gas blower 8 in pretreatment pool 2, avoids for hypoxgia.In the sewage disinfection treatment stage, main dependence microorganism is adsorbed dirty Organic substance in water and suspended substance, and what reach sewage goes nutrient laden object, has lower carbon-nitrogen ratio to make sewage after pretreatment.
In order to fully remove organism in pretreatment pool 2 and suspended substance, the residence time of sewage in pretreatment pool should between 30 minutes to 2 hours, and in pretreatment pool 2, mud should select 1-5 days age.Should be controlled within 2 by the carbon-nitrogen ratio of pretreatment pool 2 effluent sewerage, preferably be less than 1.
The sewage of being discharged by pretreatment pool 2 enters in pre-treatment settling tank 3, and realize being separated of sewage and mud, oettIed sewage enters in denitrification tank 4, and the mud after precipitation reenters in pretreatment pool 2 or enters in sludge digestion tank 6.Because the organic loading of pretreatment pool 2 is high, inevitably there is certain anaerobism and anoxic process, pretreatment pool 2 and pre-treatment settling tank 3 carry out adding a cover closed, reduce the impact of foul smell on plant area's Working environment and surrounding resident.
The sewage entered in denitrification tank 4 by pre-treatment settling tank 3 carries out denitrification process, denitrification process carries out under the condition of micro-aeration or intermittent aeration, mainly utilize the synergy of nitrite bacteria and anaerobic ammonia oxidizing bacteria, realize the removal object of nitrogen element in sewage.First the mineralized nitrogen in sewage is nitrite nitrogen by nitrite bacteria, and then ammonia nitrogen and nitrite nitrogen are together converted into nitrogen by anaerobic ammonia oxidizing bacteria, realizes the removal of nitrogen element in sewage.
In denitrification tank 4, dwell time of sewage to be littlely advisable up to 24 hours with 6, and because the generation time of anaerobic ammonia oxidizing bacteria and nitrococcus is long, in denitrification tank 4, the mud of mud age should not lower than 50 days with higher than 120 days.Denitrification tank 4 should adopt open, is conducive to nature oxic process, reduces aeration energy consumption.Denitrification tank 4 needs to establish to stir facility under water, prevents micro-aeration agitation not enough, and provides the abundant mixing of mud and sewage in the non aerated phases of intermittent aeration.
Simultaneously because the long amount of mud is few, sludge concentration is not high, and denitrification tank 4 water outlet can adopt filtering film component 5, according to circumstances, can use the methods such as settling tank yet.When other separation method of use, notice that the gas of denitrifier generation is to the air supporting effect of mud, easily causes sludge loss.Filtering film component 5 can make most of denitrifying sludge directly stay denitrification tank 4, and according to mud age, part denitrifying sludge enters denitrifying sludge storage pool 7 as excess sludge and sewage.
Organism is removed mainly through the coprecipitation mode of preprocessing process, the organism carrying suspended solids in a large amount of former water inlet enters the sludge treatment stage, in sludge digestion tank 6, adopt the mode of anaerobic digestion to stablize, and organic substance is converted into the biogas energy, supplement the energy demand of Sewage Plant.The digestion time of mud is 15 days to 100 days.The organic removal of the utility model is not blast to aeration tank the mode that air is converted into carbonic acid gas continuous in traditional technology, saves most energy expenditure.
Mud through sludge digestion tank 6 enters last disposition of solid waste, and the Digestive system containing ammonia nitrogen in high density simultaneously produced flows into denitrifying sludge storage pool 7.
The mode that denitrifying sludge storage pool 7 pairs of denitrifying sludges activity keeps is identical with denitrification tank 4, and difference is can not aeration, but the set-up mode opened wide, only provide to stir and run.It is nitrite nitrogen that nitrococcus to be used mineralized nitrogen from the oxygen of air, for anaerobic ammonia oxidizing bacteria provides matrix.
Carry denitrifying sludge from denitrification tank 4 sewage and carry the Digestive system of nutrition from sludge digestion tank 6, through mud-water separation and process, mud can be stored in denitrifying sludge storage pool 7 for a long time.Denitrifying sludge storage pool 7 regularly stops stirring, and sewage is flowed out and enters waste water processes.Because denitrification process is a gas generation process, the water outlet of denitrifying sludge storage pool 7 should be located at the middle part in pond.
From entirety, the nitrogen element flowing into Sewage Plant is all transformed by denitrifying sludge, removes.Deliquescent nitrogen element is directly removed at denitrification tank.And the organonitrogen of solid part is pretreated is trapped in sludge digestion tank 6, in the process of the digested process of pre-treatment excess sludge, be converted into deliquescent ammonia nitrogen greatly, first Digestive system flows into denitrifying sludge storage pool 7, time maintain the activity of denitrogenation excess sludge, process pollutent, then foldback flows into waste water processes simultaneously.
First the mud preserved in denitrifying sludge storage pool 7 be used as to maintain the operation of Sewage Plant self, can according to circumstances, and because of to burst accident, such as denitrifying sludge runs off, and the amount of disposing of sewage increase, concentration increases.It can be other Sewage Plant inoculation denitrifying sludge simultaneously.
From entirety, organism is removed mainly through the mode of precipitation, and the organic pollutant in water inlet enters the mode using anaerobism in the sludge treatment stage, is converted into the energy, can bring considerable self electric quantity consumption for Sewage Plant.And blast to aeration tank the mode that air is converted into carbonic acid gas continuous in unconventional process, save most energy expenditure.
Unique distinction of the present utility model is: nitrogen removal stage, and the main denitrogenation relying on anaerobic ammonia oxidizing bacteria, the nitrogen element overwhelming majority of nitrogen removal stage is converted into nitrogen, really have left water body and sludge part.Because the doubling time of microorganism is long, sludge yield is minimum, microbiologically stabilised, mainly be stored, the Digestive system simultaneously produced from sludge thickener, remove ammonia nitrogen in high density liquid, stop in the past in sewage treatment process sludge-digestion liquid return sewage treatment process, increase the shortcoming of processing load.
Claims (6)
1. one kind adopts pre-treatment and micro-aeration two benches formula less energy-consumption Sewage treatment systems, it is characterized in that: comprise pretreatment pool (2), pre-treatment settling tank (3), denitrification tank (4), gas blower (8), controller (9) and detector (10), the outlet of pretreatment pool communicates with the import of pre-treatment settling tank, and the water outlet of pre-treatment settling tank communicates with the import of denitrification tank; Gas blower realizes the aeration of pretreatment pool (2) and denitrification tank (4), detector (10) detects the water quality that the water quality and denitrification tank (4) that are flowed to pre-treatment settling tank (3) by pretreatment pool (2) flow out, and controller (9) controls the normal operation of whole Sewage treatment systems according to the detected result of detector to water quality;
The water outlet of pretreatment pool communicates with the import of pre-treatment settling tank, and the water outlet of pre-treatment settling tank communicates with denitrification tank, and the sludge outlet of pre-treatment settling tank communicates with pretreatment pool and sludge digestion tank.The sludge outlet of denitrification tank communicates with denitrifying sludge storage pool, and the water outlet of sludge digestion tank communicates with denitrifying sludge storage pool, so that the Digestive system produced enters in denitrifying sludge storage pool; Gas blower is used for carrying out aeration operation to pretreatment pool and denitrification tank, and the draining water quality of detector to the water quality of pretreatment pool effluent sewerage and denitrification tank detects, and controller, according to the detection data of detector, controls the operation of whole Sewage treatment systems.
2. employing pre-treatment according to claim 1 and micro-aeration two benches formula less energy-consumption Sewage treatment systems, it is characterized in that: the residence time of sewage in pretreatment pool (2), the mud of pretreatment pool (2) and pre-treatment settling tank (3) middle mud selected 1 ~ 5 day age between 30min ~ 120min; Denitrification tank is provided with whipping appts in (4), and the residence time of sewage in denitrification tank (4), in denitrification tank, the mud of mud selected 50 days to 120 days age between 6h ~ 24h.
3. employing pre-treatment according to claim 1 and 2 and micro-aeration two benches formula less energy-consumption Sewage treatment systems, it is characterized in that: comprise sludge digestion tank (6) and denitrifying sludge storage pool (7), the import of sludge digestion tank (6) communicates with the sludge outlet of pre-treatment settling tank (3), so that the mud that pre-treatment settling tank (3) is discharged enters in sludge digestion tank (6); Mud adopts the mode of anaerobically fermenting to stablize in sludge digestion tank (6), and organic substance is converted into the biogas energy, and the mud in sludge digestion tank is as disposition of solid waste;
The liquid exit of sludge digestion tank (6) communicates with the import of denitrifying sludge storage pool (7), so that the Digestive system containing ammonia nitrogen in high density enters in denitrifying sludge storage pool (7); The sludge outlet of denitrification tank (4) communicates with the mud import of denitrifying sludge storage pool (7), so that the mud in denitrification tank enters in denitrifying sludge storage pool.
4. employing pre-treatment according to claim 3 and micro-aeration two benches formula less energy-consumption Sewage treatment systems, it is characterized in that: the treatment time of mud in sludge digestion tank (6) is 15 days to 100 days, denitrifying sludge storage pool is provided with whipping appts in (7), and the sewage produced when denitrifying sludge storage pool (7) stops stirring enters in pretreatment pool (2) through water outlet; The mud that denitrifying sludge storage pool (7) produces is used as the operation maintaining Sewage Plant self, also can be used as the inoculation denitrifying sludge of other Sewage Plant simultaneously.
5. employing pre-treatment according to claim 1 and 2 and micro-aeration two benches formula less energy-consumption Sewage treatment systems, is characterized in that: the front end of described pretreatment pool (2) is also provided with the pretreatment pool (2) regulated water quality and the water yield for the treatment of sewage; Be provided with the filtering film component of most of sludge retention in denitrification tank in denitrification tank (4), realize being separated completely of water body and mud, also ensure that the enrichment of denitrifier.
6. employing pre-treatment according to claim 1 and 2 and micro-aeration two benches formula less energy-consumption Sewage treatment systems, is characterized in that: the carbon-nitrogen ratio being flowed into denitrification tank (4) sewage by pre-treatment settling tank (3) is less than 2; If denitrification tank (4) adopts micro-Air Exposure, the dissolved oxygen in sewage controls below 0.5, if denitrification tank adopts the method for intermittent aeration, wherein aeration phase dissolved oxygen maintains less than 2.
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| CN201520250076.XU CN204661498U (en) | 2015-04-23 | 2015-04-23 | Adopt pre-treatment and micro-aeration two benches formula less energy-consumption Sewage treatment systems |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104961290A (en) * | 2015-04-23 | 2015-10-07 | 戚汝常 | Method and system for low energy consumption sewage treatment with two stages of pretreatment and micro aeration |
| CN110862190A (en) * | 2019-11-21 | 2020-03-06 | 福建省融旗建设工程有限公司 | Septic tank adopting pretreatment and biological contact and sewage treatment method |
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2015
- 2015-04-23 CN CN201520250076.XU patent/CN204661498U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104961290A (en) * | 2015-04-23 | 2015-10-07 | 戚汝常 | Method and system for low energy consumption sewage treatment with two stages of pretreatment and micro aeration |
| CN104961290B (en) * | 2015-04-23 | 2018-04-27 | 戚汝常 | Using pretreatment and micro- aeration two benches formula low energy consumption sewage water treatment method and system |
| CN110862190A (en) * | 2019-11-21 | 2020-03-06 | 福建省融旗建设工程有限公司 | Septic tank adopting pretreatment and biological contact and sewage treatment method |
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Granted publication date: 20150923 Effective date of abandoning: 20180427 |