CN204265615U - A kind of bioelectric detecting original position clears up the waste disposal plant of mud - Google Patents
A kind of bioelectric detecting original position clears up the waste disposal plant of mud Download PDFInfo
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Abstract
Bioelectric detecting original position clears up a waste disposal plant for mud, and the utility model comprises ozone micro-nano bubble oxidation unit, the photochemical device of caryoplasm, anoxic anaerobic pond, Aerobic Pond, settling tank, clear water sterilization pool and electrical equipment automatic control cabinet, excess sludge pond mud return line respectively bubble oxidation unit micro-nano with ozone and anoxic anaerobic pond is connected, the connection of the photochemical device of caryoplasm and excess sludge settling tank, the inlet pipe of ozone micro-nano bubble oxidation unit device photochemical with caryoplasm and conventional sewage treatment unit sewage is respectively connected, the photochemical device of caryoplasm is connected with conventional sewage treatment unit anoxic anaerobic pond inlet pipe, anoxic anaerobic pond outlet pipe is connected with Aerobic Pond inlet pipe, Aerobic Pond is connected with settling tank, Aerobic Pond is connected with anoxic anaerobic pond, anoxic anaerobic pond bed mud is connected with the micro-nano bubble oxidation unit of ozone, settling tank is connected with clear water sterilization pool, be connected with mud silty sand mummifying pool at the bottom of settling tank pond.Each parts control automatic operation by electrical equipment automatic control cabinet.
Description
Technical field
The utility model belongs to sludge organism treatment process technical field, especially relevant with the waste disposal plant that a kind of bioelectric detecting original position clears up mud.
Background technology
Day by day serious along with water pollutions, carries out cost-effective process to various sewage imperative.Existing ten hundreds of sewage work runs in current global range, and more Sewage Plant will be had to be about to build along with the raising of Environmental awareness and environmental requirement.Biological sewage treatment is widely used in sewage disposal with efficient outstanding advantages, achieves immense success with the biologic process for treating sewage that active sludge and microbial film are representative in water pollution control.But, existing biologic process for treating sewage imperfection.In actual moving process, most biological sewage treatment factory faces following problem:
(1) flooding quantity is not enough, causes, affect the operation of waste disposal plant primarily of advanced planning and foul water system fault; (2) influent quality amount is unstable, and major cause is the living habit change etc. that trade effluent enters pipe network and Holidays and seasonal variation etc. and causes, and can impact loading effects wastewater treatment efficiency; (3) carbon source is not enough, the problem of this institute of Shi Ge sewage work facing, caused by modern life custom, can cause the biological unbalance removal effect affecting nitrogen and phosphorus of nutrition.
When in the face of these problems, traditional activated sludge process exposed day by day goes out following defect: in (1) aeration tank, biological concentration is low; (2) resistance to water quality, water yield impact load ability, runs stable not; (3) easily sludge bulking is produced; (4) sludge yield is large; (5) capital construction and working cost high, floor space is large.The most prominent problem of existing biologic process for treating sewage is exactly the generation of a large amount of excess sludge.The height of the expense exception of sludge treatment, accounts for greatly construction of wastewater treatment plant and runs about 50% ~ 60% of total expenses.Excess sludge needs to carry out the working cost that thus necessary disposal adds sewage disposal.As shown in figures 1 to 6, the common sludge reduction method of tradition has: anaerobic digestion and aerobic sigestion, sludge hot facture (such as wet oxidation process), sludge condensation method (such as gravity concentration method and air supporting method of enrichment), sludge dewatering method (such as mechanical dehydration and chemical coagulation process), sludge drying method (such as natural mummification method and oven drying method), and these sludge reduction methods solve mud discharging completely and dispose some drawbacks existed.
Chinese patent application (publication number CN101481191A) discloses a kind of sewage water treatment method of sludge return digestion decrement, wherein excess sludge to be returned in anaerobic precipitation pond at the precipitating sludge district long term accumulation of bottom, anaerobic precipitation pond so that by sludge digestion decrement, sewage is purified water and excess sludge by carrying out sewage disposal behind anaerobic precipitation pond, and undigested sludge needs regularly to draw clearly.
U.S. Patent application (publication number US2002/0030003A1) also discloses a kind of activated sludge sewage processing system and method, wherein in contact tank, use sludge treatment sewage, then separated sludge and water in solid-liquid separator, the mud and the part of contaminated water that are separated mixs in digester also that aeration is to make sludge digestion decrement, and the muddy water mixed solution part through aeration returns the discharge of contact tank part.
In addition, general not good to the removal effect of phosphorus in existing biologic process for treating sewage.Phosphorus is the Main Factors causing body eutrophication, and is the important element of human kind sustainable development, therefore the current control increasingly stringent to phosphorus content in water body, and turns to " recovery " from single " removal " gradually.Current dephosphorization technology is all generally after anaerobic phosphorus release, take the photograph phosphorus based on polyP bacteria under good oxygen condition by microorganism excess, therefore only has and discharges a certain amount of excess sludge to realize dephosphorization, which results in and be difficult to realize the maximized decrement of original position mud.
In sum, be badly in need of the new biological method for treating waste water of research and development and in sewage treatment process, synchronously complete the whole of organic sludge clearing up process, be only really perfect biologic process for treating sewage.
Utility model content
The purpose of this utility model is to provide a kind of bioelectric detecting original position to clear up the waste disposal plant of mud, and the utility model solves above-mentioned every deficiency that a large amount of excess sludges produce, existing biologic process for treating sewage exists and the general not good problem of the dephosphorization effect that biologic process for treating sewage exists of the existence of existing activated sewage treatment process.
For this reason, the utility model is by the following technical solutions: a kind of bioelectric detecting original position clears up the waste disposal plant of mud, it is characterized in that, described waste disposal plant comprises ozone micro-nano bubble oxidation unit, the photochemical device of caryoplasm, anoxic anaerobic pond, Aerobic Pond, settling tank, clear water sterilization pool and electrical equipment automatic control cabinet, excess sludge pond mud return line respectively bubble oxidation unit micro-nano with ozone and anoxic anaerobic pond is connected, the photochemical device of described caryoplasm is connected with excess sludge settling tank, the inlet pipe of described ozone micro-nano bubble oxidation unit device photochemical with caryoplasm and conventional sewage treatment unit sewage is respectively connected, the photochemical device of described caryoplasm is connected with conventional sewage treatment unit anoxic anaerobic pond inlet pipe, described anoxic anaerobic pond outlet pipe is connected with Aerobic Pond inlet pipe, the supernatant liquor outlet pipe of described Aerobic Pond is connected with the inlet pipe of settling tank, the bed mud return line of described Aerobic Pond is connected with anoxic anaerobic pond, described anoxic anaerobic pond bed mud return line is connected with the micro-nano bubble oxidation unit of ozone, the supernatant liquor of described settling tank is connected with clear water sterilization pool, be connected with mud silty sand mummifying pool at the bottom of described settling tank pond.Each parts control automatic operation by electrical equipment automatic control cabinet.
As to technique scheme supplement and perfect, the utility model also comprises following technical characteristic.
The utility model also comprises equalizing tank, and the effect of equalizing tank to crack cell mixture and the raw waste water intimate mixing equipment as wastewater influent.
Principle of work of the present utility model is as follows:
1st step, by the excess sludge of biological wastewater treatment process settling tank by obtain after the micro-nano bubble process of ozone broken cells decompose mixed solution, with raw waste water intimate mixing as wastewater influent, after entering anaerobic/anoxic, enter Aerobic Pond.In its operation steps, the sludge concentration of mixed solution controls to be 20000 ~ 30000mg/L.Micro-nano ozone bubbles broken cells dehydration treatment time is 0.5 ~ 2 hour, and the Dissolved Oxygen concentration Control of its mixed solution is 3 ~ 4mg/L;
2nd step, the part mixed solution broken cells by obtaining after the process of ozone micro-nano bubble being decomposed mixed solution select to turn out by the light of life the mixed solution that the photochemical microorganism of active caryoplasm obtains, and enter anaerobic/anoxic pond (also directly can enter Aerobic Pond) carry out array of biochemical reaction with raw waste water intimate mixing.In its operation steps, light source adopts the carbon fibre heating tube of far infrared rays wavelength 2.5--15 micron, and Dissolved Oxygen concentration Control is 2 ~ 3mg/L; Sludge concentration controls at 12000--16000mg/L, and the photochemical incubation time of photochemical microorganism is 12 ~ 18 hours.
3rd step, Aerobic Pond is reacted after the mixed solution that obtains carry out separation and obtain supernatant liquor and concentrated mixed solution.In its operation steps, the anaerobic/anoxic treatment time is 0.8 ~ 4 hour; Anaerobic/anoxic process realizes with coprecipitation mode, and sludge concentration controls at 3500--30000mg/L; Aerobic Pond reaction times 2-6 hour, aerobic treatment realizes in micro-nano atmospheric oxygen bubble mode, and sludge concentration controls at 4200--8500mg/L.
4th step, the 3rd step is separated the supernatant liquor obtained and discharges, concentrated mixed solution returns execution the 1st step and the 2nd step by step rapid.In its operation steps, returned sluge returns the 90-95% that the sludge quantity of the concentrated mixed solution of the 1st step is excess sludge total amount, and the sludge quantity returning the concentrated mixed solution of the 2nd step is the 5-10% of excess sludge total amount.
5th step, the 3rd step is separated the supernatant liquor purifying sterilizing process obtained discharges as water outlet, at the bottom of concentrated mixing liquid pool, carry out mummification disposal with anaerobic/anoxic pond excess sludge, inorganic silty sand.Discharge as purification water outlet after being separated supernatant liquor disinfecting time 15-30 minute that obtains in its operation steps, realize with micro-nano ozone bubbles; At the bottom of concentrated mixing liquid pool, (second pond) is disposed with settling pit (preliminary sedimentation tank) excess sludge, inorganic silty sand, realizes with low temperature desiccation apparatus.
By the above-mentioned mud and sewage of circular treatment successively, mud and sewage in-situ synchronization long-term stability can be realized and run and without the need to getting rid of organic sludge, ensure sewage disposal qualified discharge simultaneously.
Use the utility model can reach following beneficial effect: the utility model forms new sewage sludge synchronous biological treatment process to be combined with various suitable biological method for treating waste water easily.The excess sludge that biological method for treating waste water produces can by sludge digestion disposal methods of the present utility model without the need to spoil disposal.In addition, the water outlet produced by method for sludge treatment of the present utility model is usually in neutral, and namely pH value is between 6 ~ 8, therefore can reach further by advanced treatment of wastewater the water outlet meeting emission standard without the need to adjust ph.Compared with traditional wastewater bioremediation, the biological synchronization processing method of new sewage sludge can significantly reduce eliminates mud discharging even completely, capacity of resisting impact load and operation stability higher, there is good wastewater treatment efficiency and effluent quality, occupation area of equipment be little, construction cost and running cost low.Mud and sewage synchronous biological treatment process of the present utility model is particularly suitable for transforming various existing biological sewage treatment device, realizes significantly reducing eliminating organic sludge discharge even completely.
Accompanying drawing explanation
Fig. 1 is a kind of process schematic representation of existing activated sludge process.
Fig. 2 is a kind of process schematic representation of existing activated sludge process.
Fig. 3 is a kind of process schematic representation of existing activated sludge process.
Fig. 4 is a kind of process schematic representation of existing activated sludge process.
Fig. 5 is a kind of process schematic representation of existing activated sludge process.
Fig. 6 is a kind of process schematic representation of existing activated sludge process.
Fig. 7 is anatomical connectivity schematic diagram of the present utility model.
Fig. 8 is principle of work schematic diagram of the present utility model.
Fig. 9 is the utility model testing data figure.
Figure 10 is the utility model testing data figure.
Embodiment
Below in conjunction with accompanying drawing, embodiment of the present utility model is described in detail.
Embodiment: as shown in Figs. 7-8, the utility model ozone micro-nano bubble oxidation unit 2, the photochemical device 4 of caryoplasm, anoxic anaerobic pond 5, Aerobic Pond 6, settling tank 7, clear water sterilization pool 8 and electrical equipment automatic control cabinet, excess sludge pond 3 mud return line respectively bubble oxidation unit 2 micro-nano with ozone and anoxic anaerobic pond 5 is connected, the photochemical device 4 of described caryoplasm is connected with excess sludge settling tank, the inlet pipe 1 of described ozone micro-nano bubble oxidation unit 2 device 4 photochemical with caryoplasm and conventional sewage treatment unit sewage is respectively connected, the photochemical device 4 of described caryoplasm is connected with conventional sewage treatment unit anoxic anaerobic pond 5 inlet pipe, described anoxic anaerobic pond 5 outlet pipe is connected with Aerobic Pond 6 inlet pipe, the supernatant liquor outlet pipe of described Aerobic Pond 6 is connected with the inlet pipe of settling tank 7, the bed mud return line of described Aerobic Pond 6 is connected with anoxic anaerobic pond 5, described anoxic anaerobic pond 5 bed mud return line is connected with the micro-nano bubble oxidation unit 2 of ozone, the supernatant liquor of described settling tank 7 is connected with clear water sterilization pool 8, be connected with mud silty sand mummifying pool 9 at the bottom of described settling tank 7 pond, each parts control automatic operation by electrical equipment automatic control cabinet.
The utility model also comprises equalizing tank, and the effect of equalizing tank to crack cell mixture and the raw waste water intimate mixing equipment as wastewater influent.
Principle of work of the present utility model is as follows:
1st step, by the excess sludge of biological wastewater treatment process settling tank by obtain after the micro-nano bubble process of ozone broken cells decompose mixed solution, with raw waste water intimate mixing as wastewater influent, after entering anaerobic/anoxic, enter Aerobic Pond.In its operation steps, the sludge concentration of mixed solution controls to be 20000 ~ 30000mg/L.Micro-nano ozone bubbles broken cells dehydration treatment time is 0.5 ~ 2 hour, and the Dissolved Oxygen concentration Control of its mixed solution is 3 ~ 4mg/L;
2nd step, the part mixed solution broken cells by obtaining after the process of ozone micro-nano bubble being decomposed mixed solution select to turn out by the light of life the mixed solution that the photochemical microorganism of active caryoplasm obtains, and enter anaerobic/anoxic pond (also directly can enter Aerobic Pond) carry out array of biochemical reaction with raw waste water intimate mixing.In its operation steps, light source adopts the carbon fibre heating tube of far infrared rays wavelength 2.5--15 micron, and Dissolved Oxygen concentration Control is 2 ~ 3mg/L; Sludge concentration controls at 12000--16000mg/L, and the photochemical incubation time of photochemical microorganism is 12 ~ 18 hours.
3rd step, Aerobic Pond is reacted after the mixed solution that obtains carry out separation and obtain supernatant liquor and concentrated mixed solution.In its operation steps, the anaerobic/anoxic treatment time is 0.8 ~ 4 hour; Anaerobic/anoxic process realizes with coprecipitation mode, and sludge concentration controls at 3500--30000mg/L; Aerobic Pond reaction times 2-6 hour, aerobic treatment realizes in micro-nano atmospheric oxygen bubble mode, and sludge concentration controls at 4200--8500mg/L.
4th step, the 3rd step is separated the supernatant liquor obtained and discharges, concentrated mixed solution returns execution the 1st step and the 2nd step by step rapid.In its operation steps, returned sluge returns the 90-95% that the sludge quantity of the concentrated mixed solution of the 1st step is excess sludge total amount, and the sludge quantity returning the concentrated mixed solution of the 2nd step is the 5-10% of excess sludge total amount.
5th step, the 3rd step is separated the supernatant liquor purifying sterilizing process obtained discharges as water outlet, at the bottom of concentrated mixing liquid pool, carry out mummification disposal with anaerobic/anoxic pond excess sludge, inorganic silty sand.Discharge as purification water outlet after being separated supernatant liquor disinfecting time 15-30 minute that obtains in its operation steps, realize with micro-nano ozone bubbles; At the bottom of concentrated mixing liquid pool, (second pond) is disposed with settling pit (preliminary sedimentation tank) excess sludge, inorganic silty sand, realizes with Low Temperature Thermal switch.
By the above-mentioned mud and sewage of circular treatment successively, mud and sewage in-situ synchronization long-term stability can be realized and run and without the need to getting rid of organic sludge, ensure sewage disposal qualified discharge simultaneously.
Complete bioelectric detecting of the present utility model clears up mud and device independently can carry out sludge treatment, also following biologic process for treating sewage can be embedded in, realize the process of mud and sewage in-situ synchronization: A/O technique, A2/0 technique, inversion A 2/0 technique, Wuhrmann technique, SBR technique, MSBR technique, Bardenpho technique, TNCU technique, Phoredox technique, UCT technique, MUCT technique, VIP technique, OWASA technique, JHB technique, Dephanox technique, BCFS technique, adsorption biodegradation, oxidation ditch process, biomembrane process, the biologic process for treating sewage of thermopnore technique or its combination.
Principle of design of the present utility model: 1, enhancement microbiological: the microorganism that natural system exists non-fully is the most effective microorganism.Sludge digestion microorganism is through the header microorganism group army of screening, it can keep self strong activity that can activate again Natural strains, optimize and control the balance of microbial population, increase the kind of EM bacterium (probiotics) in expansion system, concentration and metabolic activity, and the growth of PM bacterium (harmful bacteria) can be suppressed.
2, the effect of enzyme: generate a large amount of hydrolysis extracellular enzymes by selecting the superior microorganism cultivated, the effect of enzyme to promote in sewage that macromolecular organism comprises dead microorganism (mud) to be broken down into small organic molecule, and discharge in conjunction with oxygen.These simple small organic molecules so by multiple-microorganism as substrate utilization, thus reach and reduce the object of surplus sludge volume.
3, biosynthesizing oxidation: activated sludge process utilizes natural microbial population to be available small organic molecule, CO2 and water to the metabolism of organic carbon by oxidation operation.In active sludge, growth phase can reduce by the organism of 40%, and the organic carbon simultaneously in organism also can carry out metabolism as the substrate of microorganism, therefore, will reduce the output of mud.Such as, in sink drainage 1000g nutrition in be used for synthesized micro-organism and about consume 600g organism, simultaneously 400g organism of having an appointment and be oxidized to CO2 and H2O.Increase and a large amount of hydrolysis extracellular enzymes that newborn enhanced biological bacterium produces only for dead or old and feeble cell works, affecting cells that can not be high to activity, this is also excess sludge reduction and not one of reason affecting effluent quality.
4, improve living microorganism concentration, extend sludge age: after newly-increased microorganism, improve the concentration of living microorganism, reduce sludge loading, and part microorganism consumes organism by endogenous respiration, mud generation is naturally corresponding minimizing also.The corresponding minimizing of surplus sludge volume can be made by sludge yield minimizing nature and extend sludge age, prolongation due to sludge age is that the cell by being hydrolyzed death or aging realizes, therefore can not affect sludge activity, the ratio of living microorganism in mud can be improved on the contrary.
5, microorganism predation effect: due to the biotransformation of poor efficiency, energy can lose to the transmittance process of high trophic level from low nutrition level, and therefore, maximizing consumption is that the maximum and biological generation of amount of power loss is minimum.Around this principle, lengthen food chain, promote the biological growth of predator bacteria, be conducive to increasing power loss, reduce the quantity of synthesising biological body.Protozoon and metazoan are the predators in active sludge, and the growth cycle of this kind of biology is far longer than the microbial growth cycle.In traditional Sludge System, because sludge age is too short, their amount will be considerably less, and predation is just little.Increase and to extend active sludge age after microorganism, increase protozoon and metazoan to dead and old and feeble microorganism predation, thus decrease surplus sludge volume.
6, the biological photochemical technology of caryoplasm: the compounding technology that " caryoplasm biology is photochemical " is collection prokaryotic organism, photosynthesis, trace element, power and water, organism high energy are oxidized to one.Its principle is the energy utilizing far infrared rays wavelength 2.5--15 micron carbon fibre heating tube, protokaryon photosynthetic microorganism is activated under power and water, select to turn out the photochemical microorganism of active caryoplasm by the light of fertility, closely tame into double oxygen osculant limit photosynthetic microorganism, intervening microorganism monoid is utilized to produce multiple higher acid in the process of decomposing organic matter, promote that in water, other sections belong to the microorganisms reproduction activation of planting, form active balance biological floe, utilize the high reactivity of osculant limit microorganism, the feature that stability and the length of time are grown, by the organic pollution materials under Anoxic/Aerobic condition successively in the effective degradation water of chain circulation continuous, excess sludge (comprising dead mud).
7, ozone micro bubble degraded sludge technology principle: ozone has the unstable organism of oxidative degradation, penetrates the function of biological activity cell, can realize sludge dewatering and disintegrate.Traditional technology ozone dissolved efficiency in water is extremely low, can not meet the demand of oxidative degradation mud.Use micro bubble means can improve the solubleness of ozone in water, make Measuring Ozone Concentration in Water reach more than 6 times of conventional value, and ozone micro bubble residence time in water is very long, can meet the demand of oxidative degradation mud.Micro bubble is produced by liquid at high speed rotary compression, has high-energy, directly can break the weave construction of the goods and materials such as cell, polymer, colloid, crack water of constitution.
In traditional various biological method for treating waste water, due to the propagation of biology, no matter whether the mud of second pond refluxes and returns to the upstream of technique, has excess sludge to discharge.With regard to whole technique, do not have the backflow reprocessing of mud owing to usually only having former the entering of water of sewage, the sludge quantity of therefore discharging always is greater than the sludge quantity of generation.In addition, must be in very low level to meet Chinese effluent requirement due to dissolved organic matter concentration in secondary clarifier effluent, aeration tank must have enough high-strength aerations and longer aeration time could reduce the concentration of dissolved organic matter in water.But under aerobic condition, low organic concentration is usually conducive to hyphomycetic propagation and causes sludge bulking.Meanwhile, high-strength aeration and long aeration time also further increase the possibility of the mixed solution generation sludge bulking containing higher concentration mud.Therefore illustrate, in traditional various activated sludge process, the sludge concentration in aeration tank is difficult to reach higher level usually, cannot realize the growth and decline equilibrium state of biological group.In addition, because biology is to the adaptability of severe environment (such as lower nutrient concentrations), sludge aerobic treatment process and sludge anaerobic treatment process only can clear up the mud of maximum 60% usually, and therefore traditional technique still needs to discharge a certain amount of excess sludge.
The utility model is as follows without the need to the reason of spoil disposal: first, because the sludge quantity of discharging is less than the sludge quantity of generation, sludge quantity in mixed solution should sustainable growth, although but the sludge concentration of mixed solution is very high but do not continue to increase but keep stable at a high level in steady running, therefore can think that the biological group in mixed solution is in the state of growth and decline balance, namely newly-increased sludge quantity is with death and the sludge quantity cleared up reaches running balance, and what thus do not have sludge quantity has a net increase of length.
At sewage sludge treatment method of the present utility model, in its biochemistry pool, the concentration of dissolved organic matter is in higher level, therefore advantageously limit hyphomycetic propagation, reduces oxygen requirement, thus when reducing aerobic treatment, the possibility of sludge bulking occurs.In addition, the dissolved organic matter of higher level is that organism provides enough nutrition, defines the environment being conducive to biological metabolism, breeding and life cycle death, make the organism in mud prolific while also in large quantities self exhaustion be destroyed.
In method for sludge treatment of the present utility model, mud alternately, repeatedly through aerobic and anoxic coupling processing, be conducive to zoogleic formation, the settling velocity of mud is improved.Therefore, method for sludge treatment of the present utility model can realize high sludge concentration and sludge bulking not occur.
In addition, make sludge age relatively long because a large amount of even all backflows of concentrated mixed solution return, the microorganism making proliferative speed slower is able to normal growth, enhances the Degradation of mud.Simultaneously under high sludge concentration condition, through aerobic and anoxic coupling processing, biodegradable thing in mixed solution and difficult for biological degradation thing (comprising dead organism) are obtained for be cleared up fast and effectively, makes the compound of carbon containing, nitrogen, phosphorus etc. become dissolved organic matter and discharges with supernatant liquor or become volatile matter and overflow.
In method for sludge treatment of the present utility model, mud in mixed solution has excellent settling property and lower oxygen requirement, and various organic substance of can degrading makes it to become water-soluble substances or gaseous substance, therefore mixed solution can have quite high sludge concentration and makes biological group be in growth and decline equilibrium state and sludge bulking does not occur, thus realizes reducing steadily in the long term even completely without the generation of excess sludge.
In sum: method for sludge treatment of the present utility model utilizes enhanced biological external source to breathe in a kind of biological wastewater treatment process and endogenous respiration degradation of organic substances and reduce the method for sludge treatment of excess sludge.That is: method for sludge treatment of the present utility model is by regulating biological physiology completely, utilizes external source to breathe and the mud in is as reflux cleared up by photochemical microbe groups in the middle of intensified type by endogenous respiration again, and realization almost produces without excess sludge.
The utility model proves in the test enforcement of several years: during in long-time running, although there is passing back in a large number of modified sewage sludge amount, sludge quantity in mixed solution still remains on metastable level and can not unrestrictedly increase, this level is by the composition of returned sluge and the impact of flow and other operational conditions, such as when wastewater influent, also by the impact of the flow of water inlet sewage, although but backflow modified sewage sludge has the carbon of high level, nitrogen and phosphorus, but carbon in the supernatant liquor of discharge, the content of nitrogen and phosphorus also can remain on lower level, this illustrates that mud and sewage synchronization processing method of the present utility model has and removes carbon significantly, the effect of nitrogen and phosphorus, can ensure that standard water discharge is discharged.
Experimental data proves: as shown in Figure 9 to find out, the sewage sludge synchronously treating sewage treatment system that application the design provides, and the COD in discharge water and ammonia nitrogen all reach GB18918-2002 one-level B standard.
Can find out as shown in Figure 10, COD, ammonia nitrogen and total phosphorus from the supernatant liquor that micro-nano ozone bubbles pond sludge digestion device is discharged are lower than the analog value of mixed solution aqueous phase significantly.Therefore, the organism that sewage and sludge reflux bring and solids can with except the forms of supernatant liquor discharge except being partially converted into, rest part all obtains in sludge digestion device to be cleared up, can show that the organism of clearing up and solids are converted into gas form and overflow in sludge digestion device, what achieve excess sludge clears up decrement.With regard to whole sewage sludge treatment device, pollution substance (main COD, ammonia nitrogen and total phosphorus) in sewage is converted into gaseous substance and overflows in sewage sludge treatment unit, while being purified water outlet, therefore do not have mud and other solid or liquid substance to discharge.The excess sludge reduction that whole Sewage treatment systems is produced even reaches sludge zero discharge.
Ultimate aim of the present utility model is without the need to spoil disposal and without sludge accumulation according to above-mentioned principle and steady in a long-term operation of mud and sewage synchronization processing method realization.Thorough solution mud discharging problem, has huge social environment and economic implications.
More than show and describe ultimate principle of the present utility model and principal character and advantage of the present utility model.The technician of the industry should understand; the utility model is not restricted to the described embodiments; what describe in above-described embodiment and specification sheets just illustrates principle of the present utility model; under the prerequisite not departing from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (2)
1. bioelectric detecting original position clears up a waste disposal plant for mud, it is characterized in that: described waste disposal plant comprises ozone micro-nano bubble oxidation unit (2), the photochemical device of caryoplasm (4), anoxic anaerobic pond (5), Aerobic Pond (6), settling tank (7), clear water sterilization pool (8) and electrical equipment automatic control cabinet; excess sludge pond (3) mud return line respectively bubble oxidation unit (2) micro-nano with ozone and anoxic anaerobic pond (5) is connected, the photochemical device of described caryoplasm (4) is connected with excess sludge settling tank, the inlet pipe (1) of described ozone micro-nano bubble oxidation unit (2) device (4) photochemical with caryoplasm and conventional sewage treatment unit sewage is respectively connected, the photochemical device of described caryoplasm (4) is connected with conventional sewage treatment unit anoxic anaerobic pond (5) inlet pipe, described anoxic anaerobic pond (5) outlet pipe is connected with Aerobic Pond (6) inlet pipe, the supernatant liquor outlet pipe of described Aerobic Pond (6) is connected with the inlet pipe of settling tank (7), the bed mud return line of described Aerobic Pond (6) is connected with anoxic anaerobic pond (5), described anoxic anaerobic pond (5) bed mud return line is connected with the micro-nano bubble oxidation unit (2) of ozone, the supernatant liquor of described settling tank (7) is connected with clear water sterilization pool (8), be connected with mud silty sand mummifying pool (9) at the bottom of described settling tank (7) pond, each parts control automatic operation by electrical equipment automatic control cabinet.
2. a kind of bioelectric detecting original position according to claim 1 clears up the waste disposal plant of mud, it is characterized in that: the utility model also comprises equalizing tank, the effect of equalizing tank to crack cell mixture and the raw waste water intimate mixing equipment as wastewater influent.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104891754A (en) * | 2015-07-09 | 2015-09-09 | 王洪臣 | Wastewater treatment process and wastewater treatment system |
| CN105543157A (en) * | 2016-01-29 | 2016-05-04 | 宁波景骐置业发展有限公司 | Screening and domesticating method of microbial flora used for purifying water quality of gardens |
| CN105800894A (en) * | 2016-05-27 | 2016-07-27 | 中山市佰明环保科技有限公司 | Sludge treatment method |
| CN110372167A (en) * | 2019-08-12 | 2019-10-25 | 杭州诚洁环保有限公司 | A kind of residual sludge reduction technique for A/O technique |
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2014
- 2014-12-05 CN CN201420761152.9U patent/CN204265615U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104891754A (en) * | 2015-07-09 | 2015-09-09 | 王洪臣 | Wastewater treatment process and wastewater treatment system |
| CN105543157A (en) * | 2016-01-29 | 2016-05-04 | 宁波景骐置业发展有限公司 | Screening and domesticating method of microbial flora used for purifying water quality of gardens |
| CN105543157B (en) * | 2016-01-29 | 2018-08-24 | 宁波景骐置业发展有限公司 | A kind of screening of microorganism species for gardens purification of water quality and acclimation method |
| CN105800894A (en) * | 2016-05-27 | 2016-07-27 | 中山市佰明环保科技有限公司 | Sludge treatment method |
| CN110372167A (en) * | 2019-08-12 | 2019-10-25 | 杭州诚洁环保有限公司 | A kind of residual sludge reduction technique for A/O technique |
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