CN209397092U - A kind of microkinetic integrated sewage treating apparatus - Google Patents

Abstract

The utility model relates to technical field of sewage, disclose a kind of microkinetic integrated sewage treating apparatus, including accommodating main body, accommodates body interior and be vertically arranged with several septic tank areas, be additionally provided with the bio-reaction zone HIBR, the settling zone HIBR, sterilization pool area and filter tank area；Septic tank area quantity is at least three, the level-one septic tank area of main center is accommodated including being located at, in the second level septic tank area and three-level septic tank area that level-one septic tank area periphery is set gradually, three septic tank areas are sequentially communicated；Three-level septic tank area, the bio-reaction zone HIBR, the settling zone HIBR, filter tank area and sterilization pool area are sequentially communicated, and filter tank area is set in sterilization pool area, after the sterilized Chi Qu processing of the water being discharged from filter tank area, are discharged by the drainpipe in sterilization pool area.The utility model structure is simple, low in cost, solves the minimum sewage handling problem for producing stain.

Description

A kind of microkinetic integrated sewage treating apparatus

Technical field

The utility model relates to technical field of sewage, relate generally to a kind of microkinetic integrated sewage treating apparatus.

Background technique

The place of the relative distributions such as rural area, tourist district belongs to minimum production stain, but these regional pipe network systems are less perfect, Sewage handling problem is not solved effectively also.Currently, the sewage that above-mentioned most area generates is using direct emission or simply Circulating water body is discharged it into after processing, the pollution of environment is destroyed greatly, is also easy the health to residence resident around It is unfavorable to cause.But for these minimum production stains, the cost for resetting pipe network solution sewage is too high, and due to these poles Abortion stain is more dispersed, is also not easy to setting pipe network.

This it is generally existing be but not yet received it is effective solve the problems, such as, it is desirable to there is method solution so that The minimum sewage treatment for producing stain in remote districts can be more efficient and convenient, reduces the destruction to environment, improves people residence Comfort.Therefore in view of the deficienciess of the prior art, needing to propose more reasonable technical solution, solution is deposited in the prior art The technical issues of.

Utility model content

The utility model provides a kind of microkinetic integrated sewage treating apparatus, it is intended to solve minimum production stain area Sewage handling problem comprehensively handles sewage using lower cost.

In order to realize said effect, the technology employed by the present utility model is

A kind of microkinetic integrated sewage treating apparatus, including main body is accommodated, the receiving body interior is longitudinally disposed There are several septic tank areas, is additionally provided with the bio-reaction zone HIBR (High efficiency integratedBiological Reactor, efficient integrated biological reaction pool), the settling zone HIBR, sterilization pool area and filter tank area；The septic tank area quantity At least three, the level-one septic tank area of main center is accommodated including being located at, in the second level that level-one septic tank area periphery is set gradually Septic tank area and three-level septic tank area, three septic tank areas are sequentially communicated；The three-level septic tank area, HIBR biological respinse Area, the settling zone HIBR, filter tank area and sterilization pool area are sequentially communicated, and filter tank area is set in sterilization pool area, are discharged from filter tank area After the sterilized Chi Qu processing of water, it is discharged by the drainpipe in sterilization pool area.

Sewage disposal device disclosed above combines septic tank, anaerobic pond, aerobic tank, sedimentation basin, filter tank and sterilization pool Occupied area together, is being saved, the mode of sewage intercepting well gravity flow enters each processing unit in equipment, this greatly reduces Power consumption, saves operating cost.Compared with traditional sewage disposal system, do not need that individual materializing strategy list is arranged Member, biological processing unit and advanced treatment unit, eliminate and take up a large area, the problem of pipeline complexity does not need power and sets Standby, structure is more simplified.

Further, since this apparatus for treating sewage is integrated with many sewage diposal areas, Shi Huizhan is designed carrying out structure Sewage disposal device disclosed in above-mentioned technical proposal is optimized to simplify occupied area with more ground space, is lifted Following feasible scheme out: the bio-reaction zone HIBR, the settling zone HIBR and the sterilization pool area is successively set on level-one The periphery in septic tank area.At work, sewage collects the three-level excrement that gravity flow after pipe network is collected enters equipment front end through system Pond, preceding three-level septic tank area main function be hydrolyzable moiety SS (suspended solids) suspended matter and decompose parasitic ovum, Changed excrement treated waste water gravity flow and enters HIBR biological reaction pool.

Further, the filter tank area in above-mentioned technical proposal is optimized, enumerates following feasible scheme: described Filter tank area use UBSF (Unpowered Biological Shallow Filter, unpowered biological shallow-layer filter tank) filter tank. The filter tank UBSF, that is, unpowered biological shallow-layer filter tank is provided with multistage filtering layer in pond, and growth has a large amount of facultative aerobes in filter layer, Nitrogen exists in the form of nitrate nitrogen in water after front-end processing, is removed by this pond nitrate nitrogen by denitrification, to guarantee total in water Nitrogen is up to standard.Suspended matter, turbidity are further removed in water while filtering.

Further, accommodate main body and be embedded in below ground, arround receive the pressure in soil, accommodate the whole of main body to improve Body intensity, while the laying of compatible each processing region, the utility model improve optimization to the structure for accommodating main body, enumerate Following feasible scheme: the middle part and lower part of the receiving main body are cylindricality, and the top for accommodating main body is diminishing cone Shape cavity, and opening is arranged in the top of cone-shaped cavity, opening is provided with top cover.

Further, above-mentioned technical proposal illustrates to accommodate the formalness of main body, and internal structure is in the formalness Under layout also corresponding optimization, specifically, enumerating following feasible scheme: the receiving body interior center is set vertically It sets cylinder body, is level-one septic tank area inside cylinder body, the longitudinally disposed several partitions of cylinder body outside wall surface simultaneously by cylinder body and hold The interval received between main body is divided into second level septic tank area, three-level septic tank area, the bio-reaction zone HIBR, the settling zone HIBR and disappears The area Du Chi.

Further, each processing region is separated by partition, and each processing region is enabled temporarily to accommodate sewage And handled, the structure of partition disclosed in above-mentioned technical proposal is optimized, following feasible scheme: institute is enumerated The height for the partition stated is equal to the height of cylinder body, is provided with overcurrent mouth on partition.

Further, the bio-reaction zone HIBR main function is to control dissolved oxygen content by adjusting aeration time, to train Corresponding active bacteria (aerobic bacteria, facultative aerobe and anaerobic bacteria) is raised, to reach removal organic polluter COD (Chemical Oxygen Demand, COD), BOD (Biochemical Oxygen Demand, biochemical oxygen demand (BOD)), ammonia nitrogen and total The purpose of phosphorus.For the work for making it keep permanently effective, the structure of bio-reaction zone is optimized, enumerates and specifically may be used as follows Capable scheme: the bio-reaction zone HIBR is provided with air-breather, and the air-breather is into the bio-reaction zone HIBR It is passed through air, is used for microorganism.

Further, the filter tank in above-mentioned technical proposal is optimized, enumerates following feasible scheme: the filter Cleaning device is provided in pond.When stopping state occurs for filtrate in filter tank, cleaning system automatically cleans filtrate, restores filter The filter capacity in pond.Water outlet takes after ultraviolet ray sterilization bactericidal direct emission or reuse i.e. according to sterilization demand after filter tank is handled It can.

Preferably, sponge is provided in the filter tank area, the cleaning device includes the water inlet being arranged in filter tank Pipe, backwash drainpipe and aerator, the shape that sponge is filled in the pond body of backwash drainpipe side and pond body is made to be in sealing State, the water of water inlet pipe protrude into the bottom of pond body by sponge；The aerator is set to bottom of pond portion, and aerator is to warp The water for crossing sponge is aerated, and reduces the density of water, water level is caused to rise, then by protruding into the backwash drainpipe of bottom of pond Discharge has achieved the purpose that cleaning with this.

Further, the filter tank area in above-mentioned technical proposal is optimized, enumerates following feasible scheme: described Filter tank in be provided with multistage filtering layer, there are the amphimicrobes of denitrification in filter layer.

Preferably, the multistage filtering layer includes the alternate spongy layer of several thicknesses, is carried out by spongy layer to water It filters, suspended matter is obstructed by sponge in water.Certain time is blocked using rear filtering layer, then is carried out in such a way that air purge adds washing Cleaning；After accumulating for a long time, a large amount of microorganism (amphimicrobe) can be grown in filter layer, waste water is carried out under simultaneous oxygen condition anti- Biological treatment is nitrified, organic pollutants and total nitrogen etc. are further removed.

Further, the bio-reaction zone HIBR and the flow-guiding structure of the settling zone HIBR are optimized, is enumerated following specific Feasible scheme: the connectivity part of the bio-reaction zone HIBR and the settling zone HIBR is provided with circular form three phase separator.

Sewage to be processed is flowed into the bio-reaction zone HIBR from three-level septic tank, with the sludge in bio-reaction zone into Row is mixed, and the air-breather by being mounted on pool bottom is aerated it, so that it is converted into gas, gas is with small Bubble form is constantly released, and micro-bubble constantly merges in uphill process, larger bubble gradually formed, on reaction tank top Three phase separator, the gas of formation are ascended into together since the agitation of gas forms a leaner sludge and water of sludge concentration When bubble encounters the reflecting plate on separator top, the surrounding of reflecting plate is folded to then from discharge suitable for reading, solid-liquid mixed liquor enters three-phase Separator, the sludge in sewage flocculate, and particle is gradually increased, and is settled under the effect of gravity, the dirt being precipitated on skew wall Mud is returned to bio-reaction zone along skew wall.

Compared with prior art, the utility model has the following beneficial effects:

1. the utility model integrates the micro- of the functional units such as materializing strategy, biological treatment, disinfection treatment, device rooms Small-scale sewage handles product, has that price is low, saving energy, occupied area are small, free from extraneous odour, that corrosion-resistant, management service is simple etc. is all More advantages.

2. a large amount of amphimicrobes grown in the multistage filtering layer that the utility model passes through the filter tank UBSF are to the water for entering filter tank In nitrate nitrogen carry out denitrification and so that effluent quality is reached " town sewage to achieve the effect that further denitrogenation Treatment plant's pollutant emission standard " (GB18918-2002) level-one A or B discharge standard, water outlet can direct emission or reuse.

Detailed description of the invention

It, below will be to use required in embodiment in order to illustrate more clearly of the technical solution of the utility model embodiment Attached drawing be briefly described, it should be understood that the following drawings only shows the section Example of the utility model, therefore does not answer Regard the restriction to range as, for those of ordinary skill in the art, without creative efforts, may be used also To obtain other relevant attached drawings according to these attached drawings.

Fig. 1 is the processing technological flow schematic diagram of sewage disposal device；

Fig. 2 is schematic diagram of internal structure when sewage disposal device is overlooked；

Fig. 3 is reserving hole arrangement schematic diagram when sewage disposal device is overlooked；

Fig. 4 is the pipeline arrangement schematic diagram of sewage disposal device；

Fig. 5 is the structural schematic diagram of the multi-bed filter in apparatus for treating sewage；

Fig. 6 is the diagrammatic cross-section in the section 1-1 in Fig. 1；

Fig. 7 is the diagrammatic cross-section in the section 2-2 in Fig. 1；

Fig. 8 is the diagrammatic cross-section in the section 3-3 in Fig. 2；

Fig. 9 is the diagrammatic cross-section in the section 4-4 in Fig. 2.

In above-mentioned attached drawing, the corresponding meaning of each label are as follows: 1, level-one septic tank area；101, level-one deflector hole；2, second level Manure pit area；201, second level deflector hole；202, slag trap；3, three-level septic tank area；301, three-level deflector hole；4, HIBR biological respinse Area；401, airport is reacted；5, the settling zone HIBR；501, transition deflector hole；6, filter tank area；7, sterilization pool area；9, aerator； 10, return pipe；11, backwash drainpipe；12, ultraviolet sterilizer；13, water inlet pipe；14, blower；15, drainpipe；16, diversion pipe； 17, water distributor；19, blind plate；20, aperture water distributor；21, sponge filler layer；22, filter plate；23, top cover；24, main body is accommodated；25, Partition；26, air-breather；27, circular form three phase separator.

Specific embodiment

With reference to the accompanying drawing and specific embodiment is further elaborated the utility model.It should be noted that right It is used to help understand the utility model in the explanation of these way of example, but does not constitute the restriction to the utility model.This Specific structure and function detail disclosed in text are only used for the example embodiment of description the utility model.However, available many alternative Form embody the utility model, and be not construed as the utility model and be limited in embodiment set forth herein.

It will be appreciated that though term first, second etc. can be used herein to describe various units, these units are not answered When being limited by these terms.These terms are only used to distinguish a unit and another unit.Such as it can be single by first Member is referred to as second unit, and similarly second unit can be referred to as first unit, without departing from showing for the utility model The range of example embodiment.

It should be appreciated that the terms "and/or", only a kind of incidence relation for describing affiliated partner, expression can be with There are three kinds of relationships, for example, A and/or B, can indicate: individualism A, individualism B exist simultaneously tri- kinds of situations of A and B, The terms "/and " are to describe another affiliated partner relationship, indicate may exist two kinds of relationships, can be with for example, A/ and B Indicate: two kinds of situations of individualism A, individualism A and B, in addition, character "/" herein, typicallying represent forward-backward correlation object is A kind of "or" relationship.

It should be appreciated that when by unit referred to as with another unit " connection ", " connected " or " coupling " when, it can with it is another A unit is directly connected or couples or temporary location may exist.Relatively, it is referred to as with another unit " directly when by unit It is connected " or when " direct-coupling ", temporary location is not present.It should explain in a similar manner for describing the relationship between unit Other words (for example, " ... between " to " between directly existing ... ", " adjacent " is to " direct neighbor " etc.).

Terms used herein are only used for description specific embodiment, and the example for being not intended to limitation the utility model is implemented Example.As it is used herein, singular "a", "an" and "the" is intended to include plural form, unless context is clear Indicate contrary.It should also be understood that term " includes ", " including ", "comprising", and/or " containing " are when used herein When, specify stated feature, integer, step, operation, unit and/or component existence, and be not excluded for one or more Other features, quantity, step, operation, unit, component and/or their combination existence or increase.

It will be further noted that the function action occurred may be with the sequence of attached drawing appearance in some alternative embodiments It is different.For example, depending on substantially being executed concurrently in related function action, or sometimes can be with Opposite sequence executes continuously show two figures.

Specific details is provided, in the following description in order to which example embodiment is understood completely.However, ability Domain those of ordinary skill is it is to be understood that implementation example embodiment without these specific details.Such as it can be System is shown in block diagram, to avoid with unnecessary details come so that example is unclear.It in other embodiments, can not be with non- Necessary details shows well-known process, structure and technology, to avoid making example embodiment unclear.

Embodiment

As shown in FIG. 1 to FIG. 9, present embodiment discloses a kind of microkinetic integrated sewage treating apparatus, including accommodate master Body 24, the receiving main body 24 use black PE (polyethylene, abbreviation PE, polyethylene) material, it is to be understood that Also other suitable materials can be used according to practical situations.If being vertically arranged with desiccation excrement inside the receiving main body 24 Chi Qu is additionally provided with the bio-reaction zone HIBR 4, the settling zone HIBR 5, sterilization pool area 7 and filter tank area 6；The septic tank area number Amount is at least three, and the level-one septic tank area 1 at 24 center of main body is accommodated including being located at, is set gradually in 1 periphery of level-one septic tank area Second level septic tank area 2 and three-level septic tank area 3, three septic tank areas are sequentially communicated；The three-level septic tank area 3, HIBR Bio-reaction zone 4, the settling zone HIBR 5, filter tank area 6 and sterilization pool area 7 are sequentially communicated, and filter tank area 6 is set in sterilization pool area 7, After the sterilized pond area 7 of the water being discharged from filter tank area 6 is handled, it is discharged by the drainpipe 15 in sterilization pool area 7.

As shown in Figure 1, sewage disposal device disclosed above, by septic tank, anaerobic pond, aerobic tank, sedimentation basin, filter tank and Sterilization pool is combined togather, and saves occupied area, and the mode of sewage intercepting well gravity flow enters each processing unit in equipment, This considerably reduce power consumptions, save operating cost.Compared with traditional sewage disposal system, it is individual setting is not needed Physicochemical treatment unit, biological processing unit and advanced treatment unit, eliminate and take up a large area, the problem of pipeline complexity, no Power-equipment is needed, structure is more simplified.

As shown in Fig. 2, designing Shi Huizhan carrying out structure since this apparatus for treating sewage is integrated with many sewage diposal areas Sewage disposal device disclosed in above-mentioned technical proposal is optimized to simplify occupied area with more ground space, is lifted Following feasible scheme out: the bio-reaction zone HIBR 4, the settling zone HIBR 5 and the sterilization pool area 7 is successively set on one The periphery in grade septic tank area 1.At work, sewage collects the three-level that gravity flow after pipe network is collected enters equipment front end through system Manure pit 3,3 main function of preceding three-level septic tank area is hydrolyzable moiety SS suspended matter and decomposes parasitic ovum, and being changed excrement, treated Waste water gravity flow HIBR biological reaction pool.

As shown in figs. 1,5 and 7, the filter tank area 6 in above-mentioned technical proposal is optimized, is enumerated following specific feasible Scheme: the filter tank area 6 uses the filter tank UBSF.The filter tank UBSF, that is, unpowered biological shallow-layer filter tank is provided with multistage in pond Filter layer, growth has a large amount of facultative aerobes in filter layer, and nitrogen exists in the form of nitrate nitrogen in the water after front-end processing, passes through this pond Nitrate nitrogen is removed by denitrification, to guarantee that total nitrogen is up to standard in water.Suspended matter, turbidity obtain further in water while filtering Removal.

Specifically, the multistage filtering layer includes the alternate spongy layer of several thicknesses, water is carried out by spongy layer It filters, suspended matter is obstructed by sponge in water.Certain time is blocked using rear filtering layer, then is carried out in such a way that air purge adds washing Cleaning；After accumulating for a long time, a large amount of microorganism (amphimicrobe) can be grown in filter layer, waste water is carried out under simultaneous oxygen condition anti- Biological treatment is nitrified, organic pollutants and total nitrogen etc. are further removed.

As shown in figs. 6-9, accommodate main body 24 and be embedded in below ground, arround receive the pressure in soil, accommodated to improve The integral strength of main body 24, while the laying of compatible each processing region, the utility model carry out the structure for accommodating main body 24 It improves and optimizates, enumerate following feasible scheme: the middle part and lower part of the receiving main body 24 are cylindricality, accommodate the upper of main body 24 Portion is diminishing cone-shaped cavity, and opening is arranged in the top of cone-shaped cavity, and opening is provided with top cover 23.

Furthermore accommodating main body 24 also can be used the structure of ladder segmentation, specifically, in the present embodiment, the receiving master The height of body 24 is 1950mm, and the lower part for accommodating main body 24 is the cylindrical body of φ 1900mm, and the height of this section of cylindrical body is 1350mm；The top for accommodating main body 24 is the cylindrical body of φ 1522mm, and the height of this section of cylindrical body is 500mm.

Above-mentioned technical proposal illustrates to accommodate the formalness of main body 24, layout of the internal structure under the formalness Also corresponding optimization, specifically, enumerating following feasible scheme: 24 inner hub location of receiving main body is vertically arranged drum Body, cylinder body inside are level-one septic tank area 1, and the longitudinally disposed several partitions 25 of cylinder body outside wall surface simultaneously by cylinder body and accommodate master Interval between body 24 is divided into second level septic tank area 2, three-level septic tank area 3, the bio-reaction zone HIBR 4,5 and of the settling zone HIBR Sterilization pool area 7.

Each processing region is separated by partition 25, is enabled each processing region temporarily to accommodate sewage and is located Reason, optimizes the structure of partition 25 disclosed in above-mentioned technical proposal, enumerates following feasible scheme: it is described every The height of plate 25 is equal to the height of cylinder body, is provided with overcurrent mouth on partition 25.

Specifically, being arranged on the side wall of level-one septic tank 1 and connecting to realize the unpowered from flowing of sewage in the present embodiment The level-one deflector hole 101 of logical second level septic tank 2, aperture are φ 60mm, and distance accommodates 24 bottom 800mm of main body；In second level The second level deflector hole 201 of setting connection three-level septic tank 3, aperture are φ 60mm on the side wall of manure pit 2, and distance accommodates main body 24 Bottom 500mm；The three-level deflector hole 301 of the setting connection bio-reaction zone HIBR 4, diameter on the side wall of three-level septic tank 3 For φ 32mm, distance accommodates the bottom 1100mm of main body 24.

In three-level septic tank 3, the top of three-level deflector hole 301 is provided with slag trap 202, for blocking top floating Object；In the bio-reaction zone HIBR 4, it is provided with the diversion pipe 16 of connection three-level deflector hole 301, diversion pipe 16 is UPUC material system At DN25 pipe；And water distributor 17 is additionally provided in the bio-reaction zone HIBR 4, one end of water distributor 17 is connected to diversion pipe 16, separately One end is connected to the other positions in the bio-reaction zone HIBR 4, is reacted convenient for microorganism, and the water distributor 17 uses The pipe of DN25 made of UPVC material.

4 main function of the bio-reaction zone HIBR is to control dissolved oxygen content by adjusting aeration time, to turn out corresponding Active bacteria (aerobic bacteria, facultative aerobe and anaerobic bacteria), to reach removal organic polluter COD, BOD, ammonia nitrogen and the mesh of total phosphorus 's.For the work for making it keep permanently effective, the structure of bio-reaction zone is optimized, enumerates following feasible side Case: the bio-reaction zone HIBR 4 is provided with air-breather 26, and the air-breather 26 is into the bio-reaction zone HIBR 4 It is passed through air, is used for microorganism.

Specifically, being provided with the reaction airport outside connection in the top of the bio-reaction zone HIBR 4 in the present embodiment 401, the aperture of reaction airport 401 is φ 20mm.Meanwhile the setting connection filter tank area 6 in the side wall surface of the settling zone HIBR 5 Transition deflector hole 501, aperture are φ 32mm, and distance accommodates the bottom 1000mm of main body 24.

Filter tank in above-mentioned technical proposal is optimized, following feasible scheme is enumerated: setting in the filter tank area 6 There is cleaning device.When stopping state occurs for filtrate in filter tank, cleaning system automatically cleans filtrate, restores the filtering in filter tank Ability.Water outlet passes through 15 direct emission of drainpipe after taking ultraviolet ray sterilization bactericidal according to sterilization demand or leads to after filter tank is handled It crosses return pipe 10 and reuse is discharged.

In sterilization, it is specifically provided with ultraviolet disinfector in sterile zones, kills major part by way of issuing ultraviolet light Microorganism.

Specifically, being provided with sponge in the filter tank area 6, the cleaning device includes being arranged in filter tank area 6 Water inlet pipe 13, backwash drainpipe 11 and aerator 9, sponge are filled in the pond body of 11 side of backwash drainpipe and make at pond body In the state of sealing, the water of water inlet pipe 13 protrudes into the bottom of pond body by sponge；The aerator 9 is set to bottom of pond Portion, 9 pairs of aerator are aerated by the water of sponge, reduce the density of water, water level is caused to rise, then by protruding into The backwash drainpipe 11 of bottom of pond is discharged, and has achieved the purpose that cleaning with this.

The water inlet pipe 13 is fixed by blind plate 19, and blind plate 19 is fixed in the bio-reaction zone HIBR 4, sets on blind plate 19 It is equipped with the pore of φ 60mm, water inlet pipe 13 passes through pore and 13 lower end of water inlet pipe is connected with aperture water distributor 20, aperture water distributor 20 direct water towards sponge, and the lower section in filter tank area 6 is infiltrated by sponge；The sponge uses the sponge filler layer of 20-40 mesh The interval of sponge filler layer 21 of 21 and 10-12 mesh is stacked；Filter plate 22 is provided with below spongy layer, the filter plate 22 uses PP material is made, and several filter seams is arranged on filter plate 22, filtering width, position of seam etc. can be arranged according to actual needs.

Above-mentioned aerator 9 is connected to external blower 14, and outer fan 14 constantly blasts gas to aerator 9, makes to expose Device of air 9 realizes the adjustment of water density, and auxiliary cleaner cleans filter tank inside.

Filter tank area 6 in above-mentioned technical proposal is optimized, enumerates following feasible scheme: in the filter tank It is provided with multistage filtering layer, there are the amphimicrobes of denitrification in filter layer.

The flow-guiding structure of the settling zone the bio-reaction zone HIBR 4 and HIBR 5 is optimized, following feasible side is enumerated Case: the connectivity part of the bio-reaction zone HIBR 4 and the settling zone HIBR 5 is provided with circular form three phase separator 27.

Sewage to be processed is flowed into the bio-reaction zone HIBR 4 from three-level septic tank 3, with the sludge in bio-reaction zone Be mixed, the air-breather 26 by being mounted on pool bottom is aerated it, so that it is converted into gas, gas with Micro-bubble form is constantly released, and micro-bubble constantly merges in uphill process, larger bubble gradually formed, in reaction tank Top ascends into three phase separator since the agitation of gas forms a leaner sludge and water of sludge concentration together, is formed Bubble when encountering the reflecting plate on separator top, be folded to the surrounding of reflecting plate then from discharge suitable for reading, solid-liquid mixed liquor enters Three phase separator, the sludge in sewage flocculate, and particle is gradually increased, and is settled under the effect of gravity, is precipitated on skew wall Sludge be returned to bio-reaction zone along skew wall.

Above-mentioned air-breather 26 is connected to external blower 14, and outer fan 14 constantly blasts gas to air-breather 26, makes Air-breather 26 realizes the concentration adjustment of mud mixture.

Specifically, the three phase separator in the present embodiment, using the three-phase separate recorded in Publication No. CN208611860U From device.

Above is the several embodiments that the utility model is enumerated, but the utility model is not limited to above-mentioned optional reality Mode is applied, in the case where not contradicting, above-mentioned technical characteristic can carry out any combination and obtain new technical solution, and this field Technical staff can obtain other numerous embodiments according to the mutual any combination of aforesaid way, anyone opens the utility model Other various forms of embodiments can be all obtained under showing.Above-mentioned specific embodiment should not be understood the guarantor of pairs of the utility model The limitation of range is protected, the protection scope of the utility model should be subject to be defined in claims, and specification can be with For interpreting the claims.

Claims (10)

1. a kind of microkinetic integrated sewage treating apparatus, it is characterised in that: including accommodating main body (24), the receiving main body (24) internal to be vertically arranged with several septic tank areas, it is additionally provided with the bio-reaction zone HIBR (4), the settling zone HIBR (5), sterilization pool Area (7) and filter tank area (6)；The septic tank area quantity is at least three, the level-one including being located at main body (24) center of receiving Manure pit area (1), in the second level septic tank area (2) and three-level septic tank area (3) that level-one septic tank area (1) periphery is set gradually, three A septic tank area is sequentially communicated；The three-level septic tank area (3), the bio-reaction zone HIBR (4), the settling zone HIBR (5), filter tank Area (6) and sterilization pool area (7) are sequentially communicated, and filter tank area (6) are set in sterilization pool area (7), the water warp being discharged from filter tank area (6) After sterilization pool area (7) processing, it is discharged by the drainpipe (15) of sterilization pool area (7).

2. microkinetic integrated sewage treating apparatus according to claim 1, it is characterised in that: the HIBR biology is anti- Area (4), the settling zone HIBR (5) and sterilization pool area (7) is answered to be successively set on the periphery in level-one septic tank area (1).

3. microkinetic integrated sewage treating apparatus according to claim 1, it is characterised in that: the filter tank area (6) Using the filter tank UBSF.

4. microkinetic integrated sewage treating apparatus according to claim 1, it is characterised in that: the receiving main body (24) middle part and lower part is cylindricality, accommodates the top of main body (24) as diminishing cone-shaped cavity, and the top of cone-shaped cavity Portion's setting opening, opening are provided with top cover (23).

5. microkinetic integrated sewage treating apparatus according to claim 1, it is characterised in that: the receiving main body (24) inner hub location is vertically arranged cylinder body, is level-one septic tank area (1) inside cylinder body, cylinder body outside wall surface is longitudinally set It sets several partitions (25) and the interval between cylinder body and receiving main body (24) is divided into second level septic tank area (2), three-level Manure pit area (3), the bio-reaction zone HIBR (4), the settling zone HIBR (5) and sterilization pool area (7).

6. microkinetic integrated sewage treating apparatus according to claim 5, it is characterised in that: the partition (25) Height is equal to the height of cylinder body, and partition is provided with overcurrent mouth on (25).

7. microkinetic integrated sewage treating apparatus according to claim 1, it is characterised in that: the HIBR biology is anti- Area (4) is answered to be provided with air-breather (26), the air-breather (26) is passed through air into the bio-reaction zone HIBR (4), supplies Microorganism uses.

8. microkinetic integrated sewage treating apparatus according to claim 1, it is characterised in that: be arranged in the filter tank There is cleaning device.

9. microkinetic integrated sewage treating apparatus according to claim 1, it is characterised in that: be arranged in the filter tank There is a multistage filtering layer, there are the amphimicrobes of denitrification in filter layer.

10. microkinetic integrated sewage treating apparatus according to claim 1, it is characterised in that: the HIBR biology The connectivity part of reaction zone (4) and the settling zone HIBR (5) is provided with circular form three phase separator (27).