CN208762235U

CN208762235U - A kind of biomembrane reaction of high order equipment

Info

Publication number: CN208762235U
Application number: CN201821112851.5U
Authority: CN
Inventors: 娓歌耽; 游赢
Original assignee: BEIJING HI-STANDARD ENVIRONMENTAL EQUIPMENT Co Ltd
Current assignee: BEIJING HI-STANDARD ENVIRONMENTAL EQUIPMENT Co Ltd
Priority date: 2018-07-13
Filing date: 2018-07-13
Publication date: 2019-04-19
Anticipated expiration: 2028-07-13

Abstract

The utility model relates to a kind of biomembrane reaction of high order equipment, including comprehensive integrated device and vertical multi-stage biochemical device；Vertical multi-stage biochemical device includes settling tank and one or more Biochemical pots；Sewage sequentially enters comprehensive integrated device, one or more Biochemical pots, settling tank；One or more Biochemical pots are accessed in parallel or series between comprehensive integrated device and settling tank.When the series connection of multiple Biochemical pots accesses between comprehensive integrated device and settling tank, different Biochemical pots is required to be sequentially loaded into identical or different filler according to sewage treatment, repetitious aerobic and anoxic treatment can be carried out to sewage, realize multistage nitration denitrification alternate cycles, substantially increase the nitric efficiency of system, the sewage being finally discharged can be made to reach the national standards such as level-one B, level-one A, when multiple Biochemical pot parallel connections access, a large amount of sewage can be handled simultaneously, greatly improve the treatment scale and efficiency of sewage.

Description

A kind of biomembrane reaction of high order equipment

Technical field

The utility model relates to technical field of sewage, and in particular to a kind of biomembrane reaction of high order equipment.

Background technique

With the rapid growth of China's rural economy and stepping up for rural resident's living standard, the life of rural area Sewage quantity significantly improves, and according to measuring and calculating, national domestic sewage in rural areas annual emissions are about 8,000,000,000 tons~9,000,000,000 tons, county, town, village row Water accounts for 50% or so of national total displacement.For growing sewage quantity, rural sewage treatment rate is serious stagnant Afterwards, according to statistics, the wastewater treatment rate of rural area only has 8%, and 96% village does not have discharge conduit and sewage disposal system, greatly Part of contaminated water is directly discharged into surrounding body and soil with regard to topography, causes the water environment pollutions such as river, pool and soil environment Pollution brings serious damage to Ecological Environment, directly threatens the health of mass peasants, hinders rural economy hair Exhibition.

Pay attention to avoiding with the sewage discharge collection and treatment facility building-up work of reinforcing rural area because sewage is unprocessed Direct emission and to the natural environments such as the water body of rural area, soil generate pollution effect, it is ensured that rural area the safety of water source and peasant Health is both to strengthen infrastructure in new countryside construction, promotes an important content of Village Redevelopment work, simultaneously Be also Rural Areas at Present living environment improve it is to be solved in work be most badly in need of, most urgent, most distinct issues, have important Realistic meaning.

Utility model content

By analysis, China's country sewage have small scale, wide, dispersion, water quality and quantity variation greatly, biodegradability it is good etc. Feature, and rural area inhabitants live's density is low, economic development fall behind, and most of do not have a drainage pipeline networks, at sewage centralized collection The characteristics of reason difficulty is larger, therefore should not indiscriminately imitate traditional urban sewage treatment process technology and tupe, need to be according to rural area, Combining with terrain landforms, select to adaptation to local conditions the sewage disposal technology and mode in suitable rural area, can just efficiently solve rural area dirt Water harnessing problem.

Based on above-mentioned needs, the purpose of this utility model is to provide one kind to be suitable for small treating capacity, concentration variation range The biomembrane reaction of high order equipment of biggish diversified earth's surface rural domestic sewage treatment.

Specific technical solution is as follows:

A kind of biomembrane reaction of high order equipment, including comprehensive integrated device and vertical multi-stage biochemical device；It is described vertical Multi-stage biochemical device includes settling tank and one or more Biochemical pots；Sewage sequentially enters the comprehensive integrated device, described One or more Biochemical pots and the settling tank；One or more of Biochemical pots access the comprehensive one in parallel or series Makeup is set between the settling tank.

Preferably, the tank body of the comprehensive integrated device is Horizontal cylinder tubular structure, and the cylinder of the tank body Side is provided with multiple movable manholes, and the primary wastewater influent nozzle is set to the top of the bottom cylindrical face of the tank body；

Inside the comprehensive integrated device from the primary wastewater influent nozzle side be divided into filtering area, regulatory region and Sludge memory block；It includes setting that filter device, overflow mechanism and the first movable manhole, the filter device are equipped in the filtering area Grid and its grills near primary wastewater influent nozzle；Overflow mechanism includes set on the centre of the first activity manhole Position and the external nozzle being connected with the described first movable manhole；

The regulatory region is equipped with biochemical device, aerator, lifting device, sewage backflow device and the second movable manhole； The biochemical device is set between grid and the second movable manhole, including filler and its filler frame；The lifting device includes Riser, the submersible sewage pump for being placed in the riser lowest part and the reflux valve for being placed in the riser top, the riser Outlet pipe connects the Biochemical pot of vertical multi-stage biochemical device by the second movable manhole；The aerator includes boring aeration pipe Road and gas-distributing pipe road；The lower section of the biochemical device filler is uniformly placed with boring aeration pipeline；Institute is passed through on the gas-distributing pipe road The first movable manhole is stated, and one end connects the boring aeration pipeline, the other end connects the air blower of aerator；Described point of gas Pipeline is also separately connected the boring aeration pipeline in the Biochemical pot and settling tank；The sewage backflow device includes mentioning with described Rise the sewage backflow pipe and the shut-off valve on the sewage backflow pipe that the outlet pipe of device is connected, the sewage backflow Before the effluent pipe mouth of pipe is located at the biochemical device.

Preferably, the Biochemical pot and the settling tank include cylindrical tank, rectangular top frame and ladder Desk-top overhead guard.

Preferably, the outlet pipe of the lifting device connects the water inlet pipe of the Biochemical pot by a shut-off valve.

Preferably, the cylindrical tank of the Biochemical pot is from top to bottom divided into water supply and drainage area, biochemical zone and exposure Gas area, the water supply and drainage area are divided by a partition to pool and drainage area, and the partition is extended downwardly the biochemical differentiation For aerobic region and anoxic zones, the aerobic region and anoxic zones are equipped with filler and its filler frame, the aerobic zone Aeration zone below domain is uniformly placed with boring aeration pipeline, and the area of section of the aerobic region is greater than anoxic zones, described The pack length of aerobic region is greater than anoxic zones；Aeration zone below the anoxic zones is equipped with inclined glass steel diaphragm, The surface of the glass steel diaphragm is located at the upper of the aerobic region towards the filler below the aerobic region, the water supply area Side, the drainage area is located at the top of the anoxic zones；The effluent pipe mouth of the water inlet pipe of the Biochemical pot is located at aerobic region Pool is given in top, and the water inlet pipe mouth of the outlet pipe of the Biochemical pot is located at the drainage area above the anoxic zones, the life The outlet pipe for changing tank accesses the settling tank or other described Biochemical pots.

Preferably, the cylindrical tank of the settling tank is divided into aeration reaction zone and settling zone by a partition, it is described heavy Shallow lake area is divided into clear water zone, filtering area and sludge area from top to bottom, the aeration reaction zone and filtering area be equipped with filler and Its filler frame, the water inlet pipe mouth of the settling tank are set to the top of the aeration reaction zone filler, the aeration reaction zone Boring aeration pipeline is uniformly placed with below filler；The cross-sectional area of the filtering area filler is greater than the aeration reaction zone and fills out The cross-sectional area of material, the filtering area pack length are less than the pack length of the aeration reaction zone；In the clear water zone, if There is gravity flow outlet pipe upward open at one end, the tank body connection that the other end of the gravity flow outlet pipe passes through the clear water zone is final Clear water pipeline.

Preferably, the lifting device includes two submersible sewage pumps, equipment is guaranteed using the using and the reserved interval Lifting scheme Continuous operation.

Preferably, the filler and its filler frame of the biochemical device are the gimp formula helical packing of curtain structure and its length Cube type filler frame.

Preferably, being equipped with for placing ultrasonic level gage between the sludge memory block and second manhole Three movable manholes, are kept apart between the sludge memory block and the third activity manhole by demarcation plate, the sludge is deposited Storage area is equipped with the 4th movable manhole and positioned at the dredging tube for having the 4th movable manhole, and the top of the demarcation plate is returned equipped with supernatant Circulation road.

Preferably, the filler of the Biochemical pot is the formula helical packing of curtain structure gimp.

Preferably, the cross-sectional area of the aerobic region filler of the Biochemical pot is the cross-sectional area of anoxic zones filler 2.5-4 times.

Preferably, the aerobic region pack length of the Biochemical pot is 1.5-3 times of the length of the filler of anoxic zones.

Preferably, the aerobic region pack length of the Biochemical pot is 2 times of the length of the filler of anoxic zones.

Preferably, the filtering area filler of the settling tank is inclined tube filler, the aeration reaction zone of the settling tank is filled out Material is suspension curtain structure gimp formula filler.

Preferably, the cross-sectional area of the filtering area filler of the settling tank is aeration reaction zone filler cross section 2.5-4 times of area.

Preferably, the pack length of the aeration reaction zone of the settling tank is 2-3 times of filtering area pack length.

Preferably, the air blower of the aerator is set in the overhead guard of the settling tank, and pass through gas-distributing pipe road point Not Lian Jie biochemical device, Biochemical pot aerobic region and settling tank biochemical aeration region boring aeration pipeline.

Preferably, the lower part of the filtering area of the settling tank is equipped with inclined sludge bucket.

Preferably, the settling tank further includes mud discharging device, the mud discharging device includes the nothing positioned at the sludge area Blocking sludge pump and its spoil disposal pipeline, the spoil disposal pipeline connect the dredging tube of the comprehensive integrated device.

Preferably, the boring aeration pipe road is equipped with venthole, the venthole is double in the boring aeration pipeline Top-cross is staggered hole, and blowing angle is 45 ° obliquely of horizontal direction.

Preferably, the height of the boring aeration pipeline is adjustable.

Compared with the prior art, the beneficial effects of the utility model have:

1, biomembrane multi-stage reacting device described in the utility model is that villages and small towns or other areas carry out height to black and odorous water The core equipment for imitating the Small Sewage Treatment Equipment of processing, by indirectly in the comprehensive integrated device and the settling tank Enter the multi-stage biochemical reaction that one or more Biochemical pots realize black and odorous water.

Connect and accessed between comprehensive integrated device and the settling tank when multiple Biochemical pots, to different Biochemical pots according to Sewage treatment requires to be sequentially loaded into identical or different filler, can carry out repetitious aerobic and anoxic treatment to sewage, It realizes multistage nitration denitrification alternate cycles, substantially increases the nitric efficiency of system, the sewage being finally discharged can be made to reach The national standards such as level-one B, level-one A can handle a large amount of sewage simultaneously, greatly mention when multiple Biochemical pot parallel connections access The treatment scale and efficiency of high sewage.Biomembrane multi-stage reacting device described in the utility model especially effluent quality require compared with Height, the limited region of land used, has wide prospect of the application.

2, biomembrane multi-stage reacting device described in the utility model, comprehensive integrated device are less in sewage load And sewage species it is single when can be used alone, and the multiple biochemistry of sewage is realized by the lifting device and sewage backflow device Cost of sewage disposal is saved in processing.And due to the design of reasonable water flow and aerator setting, so that the comprehensive integrated dress The filtering area and regulatory region set do not stockpile sludge.

3, biomembrane multi-stage reacting device described in the utility model, the water inlet pipe and outlet pipe of Biochemical pot are respectively arranged on The top of the aerobic region and anoxic zones, and the area ratio of aerobic region and anoxic zones is rationally set, make Biochemical pot The intracorporal sewage of tank there is similar pulling flow type flow pattern, increase the walking length of sewage, avoid short circuit, greatly improve The treatment effeciency of sewage；Simultaneously by the calculating of upflow velocity, the anoxic zone between partition and the tank body of Biochemical pot is rationally set The shape and structure in domain, so that the mixture of sludge and water can smoothly enter into next stage sewage-treatment plant, and in the aerobic region Lower section sets boring aeration pipeline, sets inclined glass steel diaphragm below anoxic zones, so that sludge yield is extremely low, very in Biochemical pot It is accumulated to realizing without sludge, thus the problem of sludge bulking is just not present.

Detailed description of the invention:

Fig. 1 is a kind of integral layout effect picture of embodiment of biomembrane reaction of high order equipment；

Fig. 2 is a kind of front sectional view of embodiment of comprehensive integrated device；

Fig. 3 is a kind of birds-eye perspective of embodiment of comprehensive integrated device；

Fig. 4 is a kind of A-A direction view of embodiment of comprehensive integrated device；

Fig. 5 is a kind of top view of embodiment of Biochemical pot；

Fig. 6 is a kind of B-B direction view of embodiment of Biochemical pot；

Fig. 7 is a kind of C-C direction view of embodiment of Biochemical pot；

Fig. 8 is a kind of D-D direction view of embodiment of Biochemical pot；

Fig. 9 is a kind of top view (removing overhead guard) of embodiment of settling tank；

Figure 10 is a kind of a-a direction view of embodiment of settling tank；

Figure 11 is a kind of b-b direction view of embodiment of settling tank；

Figure 12 is a kind of c-c direction view of embodiment of settling tank.

Each label in figure are as follows:

The comprehensive integrated device of 1-, 11- filtering area, 111- filter device, 111a- grid, 111b- grills, 112- overflow Stream device, the external nozzle of 112a-, the movable manhole of 113- first, 12- regulatory region, 121- biochemical device, 121a- biochemical device are filled out Material, 121b- biochemical device filler frame, 122- aerator, 122a- boring aeration pipeline, 122b- gas-distributing pipe road, 122c- are worn Hole is aerated frame, 123- lifting device, the first submersible sewage pump of 123a-, the first reflux valve of 123b-, the second submersible sewage pump of 123c-, 123d- the Two reflux valves, 124- sewage backflow device, 124a- sewage backflow pipe, the movable manhole of 125- second, 126- ultrasonic level gage, 127- third activity manhole, 13- sludge memory block, the movable manhole of 131- the 4th, 132- dredging tube, 133- supernatant return flow line 14- floor, 15- demarcation plate；

The first Biochemical pot of 2-, 2 '-the second Biochemical pots, 21- biochemistry tank, 211- water supply and drainage area, the biochemical zone 212-, 212a- Biochemical pot partition, 212b- aerobic region, 212c- anoxic zones, the aeration zone 213-, 213a- boring aeration pipeline, 22- Biochemical pot top frame, 23- Biochemical pot overhead guard, 24- filler, 25- filler frame, the inclined glass steel diaphragm of 26-, 27- are biochemical The water inlet pipe 27 of tank, the outlet pipe of 28- Biochemical pot；

3- settling tank, 31- precipitate tank, 31a- settling tank partition, the aeration reaction zone 31b-, the settling zone 31c-, 311- Clear water zone, 312- filtering area, 313- sludge area, 32- settling tank top frame, 33- settling tank overhead guard, 331- abat-vent, 34- is certainly Flow out water pipe, 35- filler, 351- inclined tube filler, 352- suspension curtain structure gimp formula filler, 36- boring aeration pipeline, 37- Sludge bucket, 38- mud discharging device, 381- is without blocking sludge pump, 382- spoil disposal pipeline, the water inlet pipe mouth of 39- settling tank；

4- primary wastewater influent nozzle；

Specific embodiment

As shown in figs. 1-12, a kind of biomembrane reaction of high order equipment, including comprehensive integrated device 1 and vertical multi-stage biochemistry Device；The vertical multi-stage biochemical device includes the first Biochemical pot 2 of two series connections, the second Biochemical pot 2 ' and settling tank 3； Sewage sequentially enters the comprehensive integrated device 1 by peripheral aqueduct, the first Biochemical pot 2, the second Biochemical pot 2 ' and heavy Shallow lake tank 3；According to standard of drainage or sewage load or other factors, settable one or more Biochemical pot serial or parallel connection access Between the comprehensive integrated device and the settling tank, when the series connection of multiple Biochemical pots accesses the comprehensive integrated device and institute When stating between settling tank, to different Biochemical pots according to sewage treatment require be sequentially loaded into different fillers, can to sewage into The repetitious aerobic and anoxic treatment of row, can make the sewage being finally discharged reach the national standards such as level-one B, level-one A, when more When a Biochemical pot parallel connection accesses, a large amount of sewage can be handled simultaneously, greatly improve the treatment scale and efficiency of sewage.

The tank body of the comprehensive integrated device 1 is Horizontal cylinder tubular structure, and the cylindrical side of the tank body is provided with Multiple activity manholes, the primary wastewater influent nozzle 4 are set to the top of the bottom cylindrical face of the tank body；It is described comprehensive integrated Device 1, one or more Biochemical pots, settling tank 3 are produced by glass reinforced plastic Mechanical entanglement burning into sand forming technique.

As a preferred option, as in Figure 2-4, multiple ribs are equipped in the tank body of the comprehensive integrated device 1 Plate 14, and the rigidity of glass reinforced plastic tank body can be greatly increased by burning into sand.Biomembrane reaction of high order described in the utility model Equipment can be made into it is buried, it is described activity manhole can satisfy various water inlet pipe network buried depths.

As in Figure 2-4, it is divided into inside the comprehensive integrated device 1 from primary 4 side of wastewater influent nozzle Filtering area 11, regulatory region 12 and sludge memory block 13；Filter device 111, overflow mechanism 112 and the are equipped in the filtering area 11 One movable manhole 113, the filter device 111 include the grid 111a and its grid near primary wastewater influent nozzle 4 Frame 111b；The structure of filter device 111 is simple, and can remove the bulk solid matters in sewage, guarantees subsequent each dress Set normal operation.Overflow mechanism 112 include set on the first movable 113 side wall of manhole middle position and with the described first movable people The external nozzle 112a that hole 113 is connected；The external nozzle 112a is the external nozzle of PE, can be recycled back to by buried pipeline Primary wastewater influent nozzle 4 or run-off, once there is overflow phenomena, overflow mechanism 112 can report monitoring of tools room It is alert, guaranteeing role not only is played to whole equipment, and effluent cycle can also be made to utilize, reduces water damage.The regulatory region 12 Equipped with the movable manhole 125 of biochemical device 121, aerator 122, lifting device 123, sewage backflow device 124 and second；It is described Biochemical device 121 is set between the movable manhole 125 of grid 111a and second, including filler 121a and its filler frame 121b；Institute Lifting device 123 is stated to include the first riser, be placed in the first submersible sewage pump 123a of the first riser lowest part and be placed in described the The first reflux valve 123b on one riser top, the second riser, the second submersible sewage pump 123c for being placed in the second riser lowest part And it is placed in the second reflux valve 123d on first riser top；The first submersible sewage pump 123a and second submersible sewage pump 123c guarantees equipment continuously-running using the using and the reserved interval Lifting scheme.

The outlet pipe of the lifting device 123 is set to the second movable manhole 125, and by being set to the second movable manhole 125 Connect the first Biochemical pot 2 of vertical multi-stage biochemical device；The aerator 122 includes boring aeration pipeline 122a and gas-distributing pipe Road 122b (connection relationship of the position of 122b and 122a and 122b needs to write)；Under the biochemical device filler 121a Side is uniformly placed with boring aeration pipeline 122a, and is supported by multiple boring aeration frame 122c.

The gas-distributing pipe road 122b connects the boring aeration pipeline 122a by first movable 113 one end of manhole, another The air blower of end connection aerator 122.And the gas-distributing pipe road 122b also connects the Biochemical pot 2 (2 ') and settling tank 3 Interior boring aeration pipeline.

The sewage backflow device 124 includes the sewage backflow pipe 124a being connected with the outlet pipe of the lifting device 123 And the shut-off valve on the sewage backflow pipe 124a, first riser, the upper end of the second riser are interconnected And the shut-off valve is connected, and be finally connected to the water outlet of the lifting device 123 when opening with the sewage backflow pipe 124a Pipe, top of the sewage backflow pipe 124a through the filler frame 121b, before sewage backflow to the biochemical device 121； It reacts sewage in the biochemical zone multi-reflow of the comprehensive integrated device 1, improves the purifying rate of sewage.

It is equipped between the sludge memory block 13 and the second movable manhole 125 for placing ultrasonic level gage 126 Third activity manhole 127；To monitor the intracorporal liquid level continuous time inner height variation of tank in real time.The sludge memory block 13 with Kept apart between the third activity manhole 127 by demarcation plate 15, the sludge memory block 13 is equipped with the 4th movable manhole 131 and positioned at the 4th movable manhole 131 dredging tube 132, the connection of dredging tube 132 be located at the settling tank 3 without blocking The sludge generated in biomembrane reaction of high order equipment is stored in the sludge memory block by sludge pump 381 and its spoil disposal pipeline 382 13, and pass through the described 4th 131 periodic cleaning sludge of movable manhole.Supernatant return flow line is equipped with above the demarcation plate 15 133.For the dredging tube 132 using the tubing of pressure resistance PE, supernatant return flow line 133 suitably highly ensure that tank is intracorporal The recycling of water body.The comprehensive integrated device, one or more Biochemical pot, settling tank can by be arranged it is different into Realize multipoint water feeding in water pipe position.

As a preferred option, the filler of Biochemical pot and its filler frame are the gimp formula helical packing of curtain structure and its length Cube type filler frame.Curtain structure gimp formula helical packing is by the special type with strongly hydrophilic and good sludge adhesion property Fiber is machined to be weaved, and shape in the shape of a spiral, and will hang filler parallel connection more and form Window curtain structure, filler frame Upper structure is simple, easy for installation, greatly reduces installation cost and time.

As a preferred option, as shown in figures 5-9, the first Biochemical pot 2 includes cylindrical tank 21, rectangular top frame Frame 22 and terrace overhead guard 23, the terrace overhead guard 23 can be opened and closed in outside, facilitate plant maintenance and maintenance, institute It states rectangular top frame 22 and facilitates each water pipe of arrangement, gas-distributing pipe road and mud pipe.

As a preferred option, the outlet pipe of the lifting device 123 is located at the Biochemical pot 2 by shut-off valve connection Biochemical pot water inlet pipe 27 can close shut-off valve, make sewage only when water is less or sewage quality is not in the case where too bad In comprehensive integrated 1 inside circulating purification of device and designated place is discharged by discharge pipe line.

As a preferred option, as viewed in figures 5-8, the cylindrical tank 21 of the Biochemical pot 2 is from top to bottom divided into Water supply and drainage area 211, biochemical zone 212 and aeration zone 213, the water supply and drainage area 211 by a partition 212a point for pool and Drainage area, the partition 212a, which is extended downwardly, divides the biochemical zone 212 for aerobic region 212b and anoxic zones 212c, described Aerobic region 212b and anoxic zones 212c is equipped with filler 24 and its filler frame 25, and the filler 24 of the Biochemical pot is curtain Structure gimp formula helical structure, curtain structure gimp formula helical packing is by with strongly hydrophilic and good sludge adhesion property Special fibre is machined to be weaved, and shape in the shape of a spiral, and will hang filler parallel connection more and form Window curtain structure, filler Structure is simple on frame, easy for installation, greatly reduces installation cost and time.

Aeration zone 213 below the aerobic region 212b is uniformly placed with boring aeration pipeline 213a, the aerobic zone The cross-sectional area of domain 212b is greater than the cross-sectional area of anoxic zones 212c, and the pack length of the aerobic region 212b is greater than The pack length of anoxic zones 212c；Aeration zone 213 below the anoxic zones 212c is equipped with inclined glass steel diaphragm 26, The surface of glass steel diaphragm 26 towards the filler below aerobic region 212b, for slow down the accumulation of sludge and make sludge slowly into Enter aeration zone；The water supply area is located above the aerobic region 212b, and the drainage area is located on the anoxic zones 212c Side；The effluent pipe mouth of the water inlet pipe 27 of the Biochemical pot 2 be located above the aerobic region 212b to pool, the first Biochemical pot The water inlet pipe mouth of 2 outlet pipe 28 is located at the drainage area above anoxic zones 212c, and the access of outlet pipe 28 of the first Biochemical pot 2 is heavy Shallow lake tank 3 or other Biochemical pots.Aerobic region 212b and anoxic zones 212c is separated using reasonable volume, so that dirty in Biochemical pot Mud yield is extremely low, even realizes and accumulates without sludge, thus the problem of sludge bulking is just not present.And use aerobic water inlet, anoxic The principle of water outlet makes sewage sufficiently carry out biochemical reaction in Biochemical pot 2.

As a preferred option, in the cylindrical tank 21 of the Biochemical pot 2, the cross section face of aerobic region 212b filler Product is 2.5-4 times of the cross-sectional area of anoxic zones 212c filler.

As a preferred option, the length of the aerobic region 212b filler 24 of the Biochemical pot 2 is anoxic zones 212c 1.5-3 times of the length of filler.

As a preferred option, the length of the aerobic region 212b filler 24 of the Biochemical pot 2 is anoxic zones 212c 2 times of the length of filler.Aerobic region 212b and anoxic zones 212c is divided using reasonable volume, and designs and reasonably fills out Expect length, it is not only easy to process, also make the sewage in Biochemical pot that there is pulling flow type flow pattern, increases the walking length of sewage, keep away Exempt from short circuit, greatly improves the treatment effeciency of sewage；The mixture of sludge and water can be made to can smoothly enter into simultaneously next Grade sewage-treatment plant.

As a preferred option, as shown in figs9-12, the settling tank 3 includes cylindrical tank 31, rectangular top Frame 32 and terrace overhead guard 33, the terrace overhead guard 33 are equipped with abat-vent 331, and can on the terrace overhead guard 33 To open and close in outside, facilitate plant maintenance and maintenance, the rectangular top frame 32 facilitate each water pipe of arrangement, Gas-distributing pipe road and mud pipe.

The cylindrical tank 31 of the settling tank 3 is aeration reaction zone 31b and settling zone 31c by a partition 31a points, described Settling zone 31c is divided into clear water zone 311, filtering area 312 and sludge area 313, the aeration reaction zone 31b and mistake from top to bottom Filter area 312 is equipped with filler and its filler frame, and the outlet pipe 28 of the Biochemical pot 2 connects the water inlet pipe of the settling tank 3, institute The water inlet pipe mouth 39 of settling tank 3 is stated set on the top of the filler of the aeration reaction zone 31b, the aeration reaction zone 31b's fills out 35 lower section of material is uniformly placed with boring aeration pipeline 36；It is anti-that the cross-sectional area of 312 filler of filtering area is greater than the aeration The cross-sectional area of area's 31b filler is answered, 312 pack length of filtering area is less than the aeration reaction zone 31b pack length, The clear water zone 311, equipped with gravity flow outlet pipe 34 upward open at one end, the other end of the gravity flow outlet pipe 34 passes through described The tank body of clear water zone connects final clear water pipeline.

As a preferred option, the filler of the filtering area 312 of the settling tank 3 is inclined tube filler 351, realizes mud and water Segmentation, the filler of the aeration reaction zone 31b of the settling tank are suspension curtain structure gimp formula filler 352.

As a preferred option, the air blower of the aerator 122 is set in the overhead guard 33 of the settling tank 3, and is led to Excessive air pipe 122b is separately connected the boring aeration pipeline of the boring aeration pipeline 122a of comprehensive integrated device 1, Biochemical pot 2 The boring aeration pipeline 36 of 213a and settling tank.

As a preferred option, the lower part of the filtering area 312 is equipped with inclined sludge bucket 37.

As a preferred option, the settling tank 3 further includes mud discharging device 38, and the mud discharging device 38 includes positioned at described Sludge area connects the comprehensive integrated device 1 without blocking sludge pump 381 and its spoil disposal pipeline 382, the spoil disposal pipeline 382 Dredging tube 132.

As a preferred option, the perforation of the boring aeration pipeline 122a of the comprehensive integrated device 1, Biochemical pot 2 expose Air pipe 213a, settling tank 3 boring aeration pipeline 36 on be equipped with venthole, the venthole is in the boring aeration pipeline Bilateral interlocks aperture, and blowing angle is 45 ° obliquely of horizontal direction.Venthole guarantees that filler adheres to micro- life using reasonable diameter Object oxygen demand.

As a preferred option, the height of above-mentioned boring aeration pipeline is adjustable.Convenient for making the outlet of boring aeration pipeline Hole is adjusted to suitable height, to reduce base sludge accumulation.

It is obvious to a person skilled in the art that the present invention is not limited to the details of the above exemplary embodiments, and And without departing substantially from the spirit or essential attributes of the utility model, it can realize that this is practical new in other specific forms Type.Therefore, in all respects, the present embodiments are to be considered as illustrative and not restrictive, this is practical new The range of type is indicated by the appended claims rather than the foregoing description, it is intended that containing for the equivalent requirements of the claims will be fallen in All changes in justice and range are embraced therein.It should not treat any reference in the claims as limiting Related claim.In addition, it should be understood that although this specification is described in terms of embodiments, but not each reality It applies mode only to contain an independent technical solution, this description of the specification is merely for the sake of clarity, this field skill Art personnel should consider the specification as a whole, and the technical solutions in the various embodiments may also be suitably combined, form ability The other embodiments that field technique personnel are understood that.

Claims

1. a kind of biomembrane reaction of high order equipment, which is characterized in that including comprehensive integrated device and vertical multi-stage biochemical device； The vertical multi-stage biochemical device includes settling tank and one or more Biochemical pots；Sewage sequentially enters the comprehensive integrated dress It sets, one or more of Biochemical pots and the settling tank；One or more of Biochemical pots access described comprehensive in parallel or series It closes between integrated apparatus and the settling tank.

2. biomembrane reaction of high order equipment as described in claim 1, which is characterized in that

The tank body of the comprehensive integrated device is Horizontal cylinder tubular structure, and the cylindrical side of the tank body is provided with multiple work Moving hole, the comprehensive integrated device further include the primary sewage water inlet pipe on the top of the bottom cylindrical face set on the tank body Mouthful；

The tank interior of the comprehensive integrated device is divided into filtering area, regulatory region from the primary wastewater influent nozzle side With sludge memory block；Filter device, overflow mechanism and the first movable manhole, the filter device are equipped in the filtering area includes Grid and its grills near primary wastewater influent nozzle；Overflow mechanism includes being set in the first activity manhole Between position and the external nozzle being connected with the described first movable manhole；

The regulatory region is equipped with biochemical device, aerator, lifting device, sewage backflow device and the second movable manhole；It is described Biochemical device is set between grid and the second movable manhole, including filler and its filler frame；The lifting device includes being promoted Manage, be placed in the submersible sewage pump of the riser lowest part and be placed in the reflux valve on the riser top, the water outlet of the riser Pipe connects the Biochemical pot of vertical multi-stage biochemical device by the second movable manhole；The aerator include boring aeration pipeline and Gas-distributing pipe road；The lower section of the biochemical device filler is uniformly placed with boring aeration pipeline；The gas-distributing pipe road is by described the One movable manhole, and one end connects the boring aeration pipeline, the other end connects the air blower of aerator；The gas-distributing pipe road Also the boring aeration pipeline being separately connected in the Biochemical pot and settling tank；The sewage backflow device includes filling with the promotion The sewage backflow pipe and the shut-off valve on the sewage backflow pipe that the outlet pipe set is connected, the sewage backflow pipe Before effluent pipe mouth is located at the biochemical device.

3. biomembrane reaction of high order equipment as claimed in claim 1 or 2, which is characterized in that the Biochemical pot and the precipitating Tank includes cylindrical tank, rectangular top frame and terrace overhead guard.

4. biomembrane reaction of high order equipment as claimed in claim 2, which is characterized in that the outlet pipe of the lifting device passes through One shut-off valve connects the water inlet pipe of the Biochemical pot.

5. biomembrane reaction of high order equipment as claimed in claim 3, which is characterized in that the outlet pipe of the lifting device passes through One shut-off valve connects the water inlet pipe of the Biochemical pot.

6. the biomembrane reaction of high order equipment as described in one of claim 1-2,4-5, which is characterized in that the circle of the Biochemical pot Cylindricality tank body is from top to bottom divided into water supply and drainage area, biochemical zone and aeration zone, and the water supply and drainage area is divided by a partition To pool and drainage area, the partition, which is extended downwardly, divides into aerobic region and anoxic zones, the aerobic zone for the biochemistry Domain and anoxic zones are equipped with filler and its filler frame, and the aeration zone below the aerobic region is uniformly placed with boring aeration Pipeline, the area of section of the aerobic region are greater than anoxic zones, and the pack length of the aerobic region is greater than anoxic zones；Institute It states aeration zone below anoxic zones and is equipped with inclined glass steel diaphragm, the surface of the glass steel diaphragm is towards the aerobic zone Filler below domain, the water supply area are located at the top of the aerobic region, and the drainage area is located at the upper of the anoxic zones Side；The effluent pipe mouth of the water inlet pipe of the Biochemical pot be located above aerobic region to pool, the outlet pipe of the Biochemical pot Water inlet pipe mouth is located at the drainage area above the anoxic zones, the outlet pipe of the Biochemical pot access the settling tank or it is described its His Biochemical pot.

7. biomembrane reaction of high order equipment as claimed in claim 3, which is characterized in that the cylindrical tank of the Biochemical pot by Water supply and drainage area, biochemical zone and aeration zone are divided under, the water supply and drainage area is divided by a partition to pool and row Pool, the partition, which is extended downwardly, divides into aerobic region and anoxic zones, the aerobic region and anoxic zone for the biochemistry Domain is equipped with filler and its filler frame, and the aeration zone below the aerobic region is uniformly placed with boring aeration pipeline, described The area of section of aerobic region is greater than anoxic zones, and the pack length of the aerobic region is greater than anoxic zones；The anoxic zone Aeration zone below domain is equipped with inclined glass steel diaphragm, and the surface of the glass steel diaphragm is towards below the aerobic region Filler, the water supply area are located at the top of the aerobic region, and the drainage area is located at the top of the anoxic zones；The life Change the water inlet pipe of tank effluent pipe mouth be located above aerobic region to pool, the water inlet pipe mouth position of the outlet pipe of the Biochemical pot The outlet pipe of drainage area above the anoxic zones, the Biochemical pot accesses the settling tank or other described Biochemical pots.

8. the biomembrane reaction of high order equipment as described in one of claim 1-2,4-5,7, which is characterized in that the settling tank Cylindrical tank is divided into aeration reaction zone and settling zone by a partition, and the settling zone is divided into clear water zone, mistake from top to bottom Filter area and sludge area, the aeration reaction zone and filtering area are equipped with filler and its filler frame, the water inlet pipe of the settling tank Mouth is set to the top of the aeration reaction zone filler, is uniformly placed with boring aeration pipe below the filler of the aeration reaction zone Road；The cross-sectional area of the filtering area filler is greater than the cross-sectional area of the aeration reaction zone filler, and the filtering area is filled out Expect that length is less than the pack length of the aeration reaction zone；In the clear water zone, equipped with gravity flow outlet pipe upward open at one end, The tank body that the other end of the gravity flow outlet pipe passes through the clear water zone connects final clear water pipeline.

9. biomembrane reaction of high order equipment as claimed in claim 3, which is characterized in that the cylindrical tank quilt of the settling tank One partition is divided into aeration reaction zone and settling zone, and the settling zone is divided into clear water zone, filtering area and sludge area from top to bottom, The aeration reaction zone and filtering area are equipped with filler and its filler frame, and the water inlet pipe mouth of the settling tank is set to the aeration The filler lower section of the top of reaction zone filler, the aeration reaction zone is uniformly placed with boring aeration pipeline；The filtering area is filled out The cross-sectional area of material is greater than the cross-sectional area of the aeration reaction zone filler, and the filtering area pack length is less than the exposure The pack length in solid/liquid/gas reactions area；In the clear water zone, equipped with gravity flow outlet pipe upward open at one end, the gravity flow outlet pipe The tank body that the other end passes through the clear water zone connects final clear water pipeline.

10. biomembrane reaction of high order equipment as claimed in claim 6, which is characterized in that the cylindrical tank of the settling tank Aeration reaction zone and settling zone are divided by a partition, the settling zone is divided into clear water zone, filtering area and sludge from top to bottom Area, the aeration reaction zone and filtering area are equipped with filler and its filler frame, and the water inlet pipe mouth of the settling tank is set to described The filler lower section of the top of aeration reaction zone filler, the aeration reaction zone is uniformly placed with boring aeration pipeline；The filtering The cross-sectional area of area's filler is greater than the cross-sectional area of the aeration reaction zone filler, and the filtering area pack length is less than institute State the pack length of aeration reaction zone；It is described from outflow water equipped with gravity flow outlet pipe upward open at one end in the clear water zone The tank body that the other end of pipe passes through the clear water zone connects final clear water pipeline.

11. the biomembrane reaction of high order equipment as described in one of claim 2,4-5,7,9-10, which is characterized in that the promotion Device includes two submersible sewage pumps, guarantees equipment continuous operation using the using and the reserved interval Lifting scheme.

12. biomembrane reaction of high order equipment as claimed in claim 3, which is characterized in that the lifting device includes two latent Dirt pump guarantees equipment continuous operation using the using and the reserved interval Lifting scheme.

13. biomembrane reaction of high order equipment as claimed in claim 6, which is characterized in that the lifting device includes two latent Dirt pump guarantees equipment continuous operation using the using and the reserved interval Lifting scheme.

14. biomembrane reaction of high order equipment as claimed in claim 8, which is characterized in that the lifting device includes two latent Dirt pump guarantees equipment continuous operation using the using and the reserved interval Lifting scheme.

15. the biomembrane reaction of high order equipment as described in one of claim 2,4-5,7,9-10,12-14, which is characterized in that institute The filler and its filler frame for stating biochemical device are the gimp formula helical packing of curtain structure and its cuboid-type filler frame.

16. biomembrane reaction of high order equipment as claimed in claim 3, which is characterized in that the filler of the biochemical device and its Filler frame is the gimp formula helical packing of curtain structure and its cuboid-type filler frame.

17. biomembrane reaction of high order equipment as claimed in claim 6, which is characterized in that the filler of the biochemical device and its Filler frame is the gimp formula helical packing of curtain structure and its cuboid-type filler frame.

18. biomembrane reaction of high order equipment as claimed in claim 8, which is characterized in that the filler of the biochemical device and its Filler frame is the gimp formula helical packing of curtain structure and its cuboid-type filler frame.

19. biomembrane reaction of high order equipment as claimed in claim 11, which is characterized in that the filler of the biochemical device and its Filler frame is the gimp formula helical packing of curtain structure and its cuboid-type filler frame.

20. the biomembrane reaction of high order equipment as described in one of claim 2,4-5,7,9-10,12-14,16-19, feature It is, the third activity people for placing ultrasonic level gage is equipped between the sludge memory block and the second movable manhole Hole is kept apart between the sludge memory block and the third activity manhole by demarcation plate, and the sludge memory block is equipped with 4th movable manhole and positioned at the dredging tube for having the 4th movable manhole, the top of the demarcation plate is equipped with supernatant return flow line.

21. biomembrane reaction of high order equipment as claimed in claim 3, which is characterized in that the sludge memory block and described the The third activity manhole for placing ultrasonic level gage, the sludge memory block and the third are equipped between two movable manholes Kept apart between movable manhole by demarcation plate, the sludge memory block is equipped with the 4th movable manhole and positioned at there is the 4th activity The top of the dredging tube of manhole, the demarcation plate is equipped with supernatant return flow line.

22. biomembrane reaction of high order equipment as claimed in claim 6, which is characterized in that the sludge memory block and described the The third activity manhole for placing ultrasonic level gage, the sludge memory block and the third are equipped between two movable manholes Kept apart between movable manhole by demarcation plate, the sludge memory block is equipped with the 4th movable manhole and positioned at there is the 4th activity The top of the dredging tube of manhole, the demarcation plate is equipped with supernatant return flow line.

23. biomembrane reaction of high order equipment as claimed in claim 8, which is characterized in that the sludge memory block and described the The third activity manhole for placing ultrasonic level gage, the sludge memory block and the third are equipped between two movable manholes Kept apart between movable manhole by demarcation plate, the sludge memory block is equipped with the 4th movable manhole and positioned at there is the 4th activity The top of the dredging tube of manhole, the demarcation plate is equipped with supernatant return flow line.

24. biomembrane reaction of high order equipment as claimed in claim 11, which is characterized in that the sludge memory block and described the The third activity manhole for placing ultrasonic level gage, the sludge memory block and the third are equipped between two movable manholes Kept apart between movable manhole by demarcation plate, the sludge memory block is equipped with the 4th movable manhole and positioned at there is the 4th activity The top of the dredging tube of manhole, the demarcation plate is equipped with supernatant return flow line.

25. biomembrane reaction of high order equipment as claimed in claim 15, which is characterized in that the sludge memory block and described the The third activity manhole for placing ultrasonic level gage, the sludge memory block and the third are equipped between two movable manholes Kept apart between movable manhole by demarcation plate, the sludge memory block is equipped with the 4th movable manhole and positioned at there is the 4th activity The top of the dredging tube of manhole, the demarcation plate is equipped with supernatant return flow line.

26. the biomembrane reaction of high order as described in one of claim 1-2,4-5,7,9-10,12-14,16-19,21-25 is set It is standby, which is characterized in that the filler of the Biochemical pot is the formula helical packing of curtain structure gimp.

27. biomembrane reaction of high order equipment as claimed in claim 3, which is characterized in that the filler of the Biochemical pot is curtain Structure gimp formula helical packing.

28. biomembrane reaction of high order equipment as claimed in claim 6, which is characterized in that the filler of the Biochemical pot is curtain Structure gimp formula helical packing.

29. biomembrane reaction of high order equipment as claimed in claim 8, which is characterized in that the filler of the Biochemical pot is curtain Structure gimp formula helical packing.

30. biomembrane reaction of high order equipment as claimed in claim 11, which is characterized in that the filler of the Biochemical pot is curtain Structure gimp formula helical packing.

31. biomembrane reaction of high order equipment as claimed in claim 15, which is characterized in that the filler of the Biochemical pot is curtain Structure gimp formula helical packing.

32. biomembrane reaction of high order equipment as claimed in claim 20, which is characterized in that the filler of the Biochemical pot is curtain Structure gimp formula helical packing.

33. biomembrane reaction of high order equipment as claimed in claim 6, which is characterized in that the aerobic region of the Biochemical pot is filled out The cross-sectional area of material is 2.5-4 times of the cross-sectional area of anoxic zones filler.

34. the biomembrane reaction of high order equipment as described in one of claim 7,9-10,12-14,16-19,21-25,27-32, It is characterized in that, the cross-sectional area of the aerobic region filler of the Biochemical pot is the 2.5- of the cross-sectional area of anoxic zones filler 4 times.

35. biomembrane reaction of high order equipment as claimed in claim 8, which is characterized in that the aerobic region of the Biochemical pot is filled out The cross-sectional area of material is 2.5-4 times of the cross-sectional area of anoxic zones filler.

36. biomembrane reaction of high order equipment as claimed in claim 11, which is characterized in that the aerobic region of the Biochemical pot is filled out The cross-sectional area of material is 2.5-4 times of the cross-sectional area of anoxic zones filler.

37. biomembrane reaction of high order equipment as claimed in claim 15, which is characterized in that the aerobic region of the Biochemical pot is filled out The cross-sectional area of material is 2.5-4 times of the cross-sectional area of anoxic zones filler.

38. biomembrane reaction of high order equipment as claimed in claim 20, which is characterized in that the aerobic region of the Biochemical pot is filled out The cross-sectional area of material is 2.5-4 times of the cross-sectional area of anoxic zones filler.

39. biomembrane reaction of high order equipment as claimed in claim 26, which is characterized in that the aerobic region of the Biochemical pot is filled out The cross-sectional area of material is 2.5-4 times of the cross-sectional area of anoxic zones filler.

40. biomembrane reaction of high order equipment as claimed in claim 6, which is characterized in that the aerobic region of the Biochemical pot is filled out Material length is 1.5-3 times of the length of the filler of anoxic zones.

41. the biomembrane reaction of high order as described in one of claim 7,9-10,12-14,16-19,21-25,27-33,35-39 Equipment, which is characterized in that the aerobic region pack length of the Biochemical pot is 1.5-3 times of the length of the filler of anoxic zones.

42. biomembrane reaction of high order equipment as claimed in claim 8, which is characterized in that the aerobic region of the Biochemical pot is filled out Material length is 1.5-3 times of the length of the filler of anoxic zones.

43. biomembrane reaction of high order equipment as claimed in claim 11, which is characterized in that the aerobic region of the Biochemical pot is filled out Material length is 1.5-3 times of the length of the filler of anoxic zones.

44. biomembrane reaction of high order equipment as claimed in claim 15, which is characterized in that the aerobic region of the Biochemical pot is filled out Material length is 1.5-3 times of the length of the filler of anoxic zones.

45. biomembrane reaction of high order equipment as claimed in claim 20, which is characterized in that the aerobic region of the Biochemical pot is filled out Material length is 1.5-3 times of the length of the filler of anoxic zones.

46. biomembrane reaction of high order equipment as claimed in claim 26, which is characterized in that the aerobic region of the Biochemical pot is filled out Material length is 1.5-3 times of the length of the filler of anoxic zones.

47. biomembrane reaction of high order equipment as claimed in claim 34, which is characterized in that the aerobic region of the Biochemical pot is filled out Material length is 1.5-3 times of the length of the filler of anoxic zones.

48. biomembrane reaction of high order equipment as claimed in claim 6, which is characterized in that the aerobic region of the Biochemical pot is filled out Material length is 2 times of the length of the filler of anoxic zones.

49. the biomembrane as described in one of claim 7,9-10,12-14,16-19,21-25,27-33,35-40,42-47 is more Order reaction equipment, which is characterized in that the aerobic region pack length of the Biochemical pot is the 2 of the length of the filler of anoxic zones Times.

50. biomembrane reaction of high order equipment as claimed in claim 8, which is characterized in that the aerobic region of the Biochemical pot is filled out Material length is 2 times of the length of the filler of anoxic zones.

51. biomembrane reaction of high order equipment as claimed in claim 11, which is characterized in that the aerobic region of the Biochemical pot is filled out Material length is 2 times of the length of the filler of anoxic zones.

52. biomembrane reaction of high order equipment as claimed in claim 15, which is characterized in that the aerobic region of the Biochemical pot is filled out Material length is 2 times of the length of the filler of anoxic zones.

53. biomembrane reaction of high order equipment as claimed in claim 20, which is characterized in that the aerobic region of the Biochemical pot is filled out Material length is 2 times of the length of the filler of anoxic zones.

54. biomembrane reaction of high order equipment as claimed in claim 26, which is characterized in that the aerobic region of the Biochemical pot is filled out Material length is 2 times of the length of the filler of anoxic zones.

55. biomembrane reaction of high order equipment as claimed in claim 34, which is characterized in that the aerobic region of the Biochemical pot is filled out Material length is 2 times of the length of the filler of anoxic zones.

56. biomembrane reaction of high order equipment as claimed in claim 41, which is characterized in that the aerobic region of the Biochemical pot is filled out Material length is 2 times of the length of the filler of anoxic zones.

57. biomembrane reaction of high order equipment as claimed in claim 8, which is characterized in that the filtering area filler of the settling tank For inclined tube filler, the filler of the aeration reaction zone of the settling tank is suspension curtain structure gimp formula filler.

58. the biology as described in one of claim 9-10,12-14,16-19,21-25,27-33,35-40,42-48,50-56 Film reaction of high order equipment, which is characterized in that the filtering area filler of the settling tank is inclined tube filler, and the aeration of the settling tank is anti- Answer the filler in area for suspension curtain structure gimp formula filler.

59. biomembrane reaction of high order equipment as claimed in claim 11, which is characterized in that the filtering area filler of the settling tank For inclined tube filler, the filler of the aeration reaction zone of the settling tank is suspension curtain structure gimp formula filler.

60. biomembrane reaction of high order equipment as claimed in claim 15, which is characterized in that the filtering area filler of the settling tank For inclined tube filler, the filler of the aeration reaction zone of the settling tank is suspension curtain structure gimp formula filler.

61. biomembrane reaction of high order equipment as claimed in claim 20, which is characterized in that the filtering area filler of the settling tank For inclined tube filler, the filler of the aeration reaction zone of the settling tank is suspension curtain structure gimp formula filler.

62. biomembrane reaction of high order equipment as claimed in claim 26, which is characterized in that the filtering area filler of the settling tank For inclined tube filler, the filler of the aeration reaction zone of the settling tank is suspension curtain structure gimp formula filler.

63. biomembrane reaction of high order equipment as claimed in claim 34, which is characterized in that the filtering area filler of the settling tank For inclined tube filler, the filler of the aeration reaction zone of the settling tank is suspension curtain structure gimp formula filler.

64. biomembrane reaction of high order equipment as claimed in claim 41, which is characterized in that the filtering area filler of the settling tank For inclined tube filler, the filler of the aeration reaction zone of the settling tank is suspension curtain structure gimp formula filler.

65. biomembrane reaction of high order equipment as claimed in claim 49, which is characterized in that the filtering area filler of the settling tank For inclined tube filler, the filler of the aeration reaction zone of the settling tank is suspension curtain structure gimp formula filler.

66. biomembrane reaction of high order equipment as claimed in claim 8, which is characterized in that the filtering area filler of the settling tank Cross-sectional area be 2.5-4 times of the aeration reaction zone filler cross-sectional area.

67. as described in one of claim 9-10,12-14,16-19,21-25,27-33,35-40,42-48,50-57,59-65 Biomembrane reaction of high order equipment, which is characterized in that the cross-sectional area of the filtering area filler of the settling tank is the aeration 2.5-4 times of reaction zone filler cross-sectional area.

68. biomembrane reaction of high order equipment as claimed in claim 11, which is characterized in that the filtering area filler of the settling tank Cross-sectional area be 2.5-4 times of the aeration reaction zone filler cross-sectional area.

69. biomembrane reaction of high order equipment as claimed in claim 15, which is characterized in that the filtering area filler of the settling tank Cross-sectional area be 2.5-4 times of the aeration reaction zone filler cross-sectional area.

70. biomembrane reaction of high order equipment as claimed in claim 20, which is characterized in that the filtering area filler of the settling tank Cross-sectional area be 2.5-4 times of the aeration reaction zone filler cross-sectional area.

71. biomembrane reaction of high order equipment as claimed in claim 26, which is characterized in that the filtering area filler of the settling tank Cross-sectional area be 2.5-4 times of the aeration reaction zone filler cross-sectional area.

72. biomembrane reaction of high order equipment as claimed in claim 34, which is characterized in that the filtering area filler of the settling tank Cross-sectional area be 2.5-4 times of the aeration reaction zone filler cross-sectional area.

73. biomembrane reaction of high order equipment as claimed in claim 41, which is characterized in that the filtering area filler of the settling tank Cross-sectional area be 2.5-4 times of the aeration reaction zone filler cross-sectional area.

74. biomembrane reaction of high order equipment as claimed in claim 49, which is characterized in that the filtering area filler of the settling tank Cross-sectional area be 2.5-4 times of the aeration reaction zone filler cross-sectional area.

75. biomembrane reaction of high order equipment as claimed in claim 58, which is characterized in that the filtering area filler of the settling tank Cross-sectional area be 2.5-4 times of the aeration reaction zone filler cross-sectional area.

76. biomembrane reaction of high order equipment as claimed in claim 8, which is characterized in that the aeration reaction zone of the settling tank Pack length be 2-3 times of filtering area pack length.

77. as claim 9-10,12-14,16-19,21-25,27-33,35-40,42-48,50-57,59-66,68-75 it Biomembrane reaction of high order equipment described in one, which is characterized in that the pack length of the aeration reaction zone of the settling tank is filtering 2-3 times of area's pack length.

78. biomembrane reaction of high order equipment as claimed in claim 11, which is characterized in that the aeration reaction zone of the settling tank Pack length be 2-3 times of filtering area pack length.

79. biomembrane reaction of high order equipment as claimed in claim 15, which is characterized in that the aeration reaction zone of the settling tank Pack length be 2-3 times of filtering area pack length.

80. biomembrane reaction of high order equipment as claimed in claim 20, which is characterized in that the aeration reaction zone of the settling tank Pack length be 2-3 times of filtering area pack length.

81. biomembrane reaction of high order equipment as claimed in claim 26, which is characterized in that the aeration reaction zone of the settling tank Pack length be 2-3 times of filtering area pack length.

82. biomembrane reaction of high order equipment as claimed in claim 34, which is characterized in that the aeration reaction zone of the settling tank Pack length be 2-3 times of filtering area pack length.

83. biomembrane reaction of high order equipment as claimed in claim 41, which is characterized in that the aeration reaction zone of the settling tank Pack length be 2-3 times of filtering area pack length.

84. biomembrane reaction of high order equipment as claimed in claim 49, which is characterized in that the aeration reaction zone of the settling tank Pack length be 2-3 times of filtering area pack length.

85. biomembrane reaction of high order equipment as claimed in claim 58, which is characterized in that the aeration reaction zone of the settling tank Pack length be 2-3 times of filtering area pack length.

86. the biomembrane reaction of high order equipment as described in claim 67, which is characterized in that the aeration reaction zone of the settling tank Pack length be 2-3 times of filtering area pack length.

87. biomembrane reaction of high order equipment as claimed in claim 8, which is characterized in that the air blower of the aerator is set Biochemical device, Biochemical pot aerobic region and settling tank life are separately connected in the overhead guard of the settling tank, and through gas-distributing pipe road Change the boring aeration pipeline of aerated space.

88. as claim 9-10,12-14,16-19,21-25,27-33,35-40,42-48,50-57,59-66,68-76, Biomembrane reaction of high order equipment described in one of 79-86, which is characterized in that the air blower of the aerator is set to the precipitating In the overhead guard of tank, and biochemical device, Biochemical pot aerobic region and settling tank biochemical aeration region are separately connected by gas-distributing pipe road Boring aeration pipeline.

89. biomembrane reaction of high order equipment as claimed in claim 11, which is characterized in that the air blower of the aerator is set Biochemical device, Biochemical pot aerobic region and settling tank life are separately connected in the overhead guard of the settling tank, and through gas-distributing pipe road Change the boring aeration pipeline of aerated space.

90. biomembrane reaction of high order equipment as claimed in claim 15, which is characterized in that the air blower of the aerator is set Biochemical device, Biochemical pot aerobic region and settling tank life are separately connected in the overhead guard of the settling tank, and through gas-distributing pipe road Change the boring aeration pipeline of aerated space.

91. biomembrane reaction of high order equipment as claimed in claim 20, which is characterized in that the air blower of the aerator is set Biochemical device, Biochemical pot aerobic region and settling tank life are separately connected in the overhead guard of the settling tank, and through gas-distributing pipe road Change the boring aeration pipeline of aerated space.

92. biomembrane reaction of high order equipment as claimed in claim 26, which is characterized in that the air blower of the aerator is set Biochemical device, Biochemical pot aerobic region and settling tank life are separately connected in the overhead guard of the settling tank, and through gas-distributing pipe road Change the boring aeration pipeline of aerated space.

93. biomembrane reaction of high order equipment as claimed in claim 34, which is characterized in that the air blower of the aerator is set Biochemical device, Biochemical pot aerobic region and settling tank life are separately connected in the overhead guard of the settling tank, and through gas-distributing pipe road Change the boring aeration pipeline of aerated space.

94. biomembrane reaction of high order equipment as claimed in claim 41, which is characterized in that the air blower of the aerator is set Biochemical device, Biochemical pot aerobic region and settling tank life are separately connected in the overhead guard of the settling tank, and through gas-distributing pipe road Change the boring aeration pipeline of aerated space.

95. biomembrane reaction of high order equipment as claimed in claim 49, which is characterized in that the air blower of the aerator is set Biochemical device, Biochemical pot aerobic region and settling tank life are separately connected in the overhead guard of the settling tank, and through gas-distributing pipe road Change the boring aeration pipeline of aerated space.

96. biomembrane reaction of high order equipment as claimed in claim 58, which is characterized in that the air blower of the aerator is set Biochemical device, Biochemical pot aerobic region and settling tank life are separately connected in the overhead guard of the settling tank, and through gas-distributing pipe road Change the boring aeration pipeline of aerated space.

97. the biomembrane reaction of high order equipment as described in claim 67, which is characterized in that the air blower of the aerator is set Biochemical device, Biochemical pot aerobic region and settling tank life are separately connected in the overhead guard of the settling tank, and through gas-distributing pipe road Change the boring aeration pipeline of aerated space.

98. the biomembrane reaction of high order equipment as described in claim 77, which is characterized in that the air blower of the aerator is set Biochemical device, Biochemical pot aerobic region and settling tank life are separately connected in the overhead guard of the settling tank, and through gas-distributing pipe road Change the boring aeration pipeline of aerated space.

99. biomembrane reaction of high order equipment as claimed in claim 8, which is characterized in that under the filtering area of the settling tank Portion is equipped with inclined sludge bucket.

100. as claim 9-10,12-14,16-19,21-25,27-33,35-40,42-48,50-57,59-66,68-76, Biomembrane reaction of high order equipment described in one of 78-87,89-98, which is characterized in that the lower part of the filtering area of the settling tank is set There is inclined sludge bucket.

101. biomembrane reaction of high order equipment as claimed in claim 11, which is characterized in that the filtering area of the settling tank Lower part is equipped with inclined sludge bucket.

102. biomembrane reaction of high order equipment as claimed in claim 15, which is characterized in that the filtering area of the settling tank Lower part is equipped with inclined sludge bucket.

103. biomembrane reaction of high order equipment as claimed in claim 20, which is characterized in that the filtering area of the settling tank Lower part is equipped with inclined sludge bucket.

104. biomembrane reaction of high order equipment as claimed in claim 26, which is characterized in that the filtering area of the settling tank Lower part is equipped with inclined sludge bucket.

105. biomembrane reaction of high order equipment as claimed in claim 34, which is characterized in that the filtering area of the settling tank Lower part is equipped with inclined sludge bucket.

106. biomembrane reaction of high order equipment as claimed in claim 41, which is characterized in that the filtering area of the settling tank Lower part is equipped with inclined sludge bucket.

107. biomembrane reaction of high order equipment as claimed in claim 49, which is characterized in that the filtering area of the settling tank Lower part is equipped with inclined sludge bucket.

108. biomembrane reaction of high order equipment as claimed in claim 58, which is characterized in that the filtering area of the settling tank Lower part is equipped with inclined sludge bucket.

109. the biomembrane reaction of high order equipment as described in claim 67, which is characterized in that the filtering area of the settling tank Lower part is equipped with inclined sludge bucket.

110. the biomembrane reaction of high order equipment as described in claim 77, which is characterized in that the filtering area of the settling tank Lower part is equipped with inclined sludge bucket.

111. the biomembrane reaction of high order equipment as described in claim 88, which is characterized in that the filtering area of the settling tank Lower part is equipped with inclined sludge bucket.

112. biomembrane reaction of high order equipment as claimed in claim 8, which is characterized in that the settling tank further includes spoil disposal dress It sets, the mud discharging device includes positioned at the sludge area without blocking sludge pump and its spoil disposal pipeline, the spoil disposal pipeline connection The dredging tube of the comprehensive integrated device.

113. as claim 9-10,12-14,16-19,21-25,27-33,35-40,42-48,50-57,59-66,68-76, Biomembrane reaction of high order equipment described in one of 78-87,89-99,101-111, which is characterized in that the settling tank further includes row Mud device, the mud discharging device include positioned at the sludge area without blocking sludge pump and its spoil disposal pipeline, the spoil disposal pipeline Connect the dredging tube of the comprehensive integrated device.

114. biomembrane reaction of high order equipment as claimed in claim 11, which is characterized in that the settling tank further includes spoil disposal Device, the mud discharging device include positioned at the sludge area without blocking sludge pump and its spoil disposal pipeline, and the spoil disposal pipeline connects Connect the dredging tube of the comprehensive integrated device.

115. biomembrane reaction of high order equipment as claimed in claim 15, which is characterized in that the settling tank further includes spoil disposal Device, the mud discharging device include positioned at the sludge area without blocking sludge pump and its spoil disposal pipeline, and the spoil disposal pipeline connects Connect the dredging tube of the comprehensive integrated device.

116. biomembrane reaction of high order equipment as claimed in claim 20, which is characterized in that the settling tank further includes spoil disposal Device, the mud discharging device include positioned at the sludge area without blocking sludge pump and its spoil disposal pipeline, and the spoil disposal pipeline connects Connect the dredging tube of the comprehensive integrated device.

117. biomembrane reaction of high order equipment as claimed in claim 26, which is characterized in that the settling tank further includes spoil disposal Device, the mud discharging device include positioned at the sludge area without blocking sludge pump and its spoil disposal pipeline, and the spoil disposal pipeline connects Connect the dredging tube of the comprehensive integrated device.

118. biomembrane reaction of high order equipment as claimed in claim 34, which is characterized in that the settling tank further includes spoil disposal Device, the mud discharging device include positioned at the sludge area without blocking sludge pump and its spoil disposal pipeline, and the spoil disposal pipeline connects Connect the dredging tube of the comprehensive integrated device.

119. biomembrane reaction of high order equipment as claimed in claim 41, which is characterized in that the settling tank further includes spoil disposal Device, the mud discharging device include positioned at the sludge area without blocking sludge pump and its spoil disposal pipeline, and the spoil disposal pipeline connects Connect the dredging tube of the comprehensive integrated device.

120. biomembrane reaction of high order equipment as claimed in claim 49, which is characterized in that the settling tank further includes spoil disposal Device, the mud discharging device include positioned at the sludge area without blocking sludge pump and its spoil disposal pipeline, and the spoil disposal pipeline connects Connect the dredging tube of the comprehensive integrated device.

121. biomembrane reaction of high order equipment as claimed in claim 58, which is characterized in that the settling tank further includes spoil disposal Device, the mud discharging device include positioned at the sludge area without blocking sludge pump and its spoil disposal pipeline, and the spoil disposal pipeline connects Connect the dredging tube of the comprehensive integrated device.

122. the biomembrane reaction of high order equipment as described in claim 67, which is characterized in that the settling tank further includes spoil disposal Device, the mud discharging device include positioned at the sludge area without blocking sludge pump and its spoil disposal pipeline, and the spoil disposal pipeline connects Connect the dredging tube of the comprehensive integrated device.

123. the biomembrane reaction of high order equipment as described in claim 77, which is characterized in that the settling tank further includes spoil disposal Device, the mud discharging device include positioned at the sludge area without blocking sludge pump and its spoil disposal pipeline, and the spoil disposal pipeline connects Connect the dredging tube of the comprehensive integrated device.

124. the biomembrane reaction of high order equipment as described in claim 88, which is characterized in that the settling tank further includes spoil disposal Device, the mud discharging device include positioned at the sludge area without blocking sludge pump and its spoil disposal pipeline, and the spoil disposal pipeline connects Connect the dredging tube of the comprehensive integrated device.

125. the biomembrane reaction of high order equipment as described in claim 100, which is characterized in that the settling tank further includes spoil disposal Device, the mud discharging device include positioned at the sludge area without blocking sludge pump and its spoil disposal pipeline, and the spoil disposal pipeline connects Connect the dredging tube of the comprehensive integrated device.

126. such as claim 2,4-5,7,9-10,12-14,16-19,21-25,27-33,35-40,42-48,50-57,59- 66, biomembrane reaction of high order equipment described in one of 68-76,78-87,89-99,101-112,114-125, which is characterized in that Boring aeration pipe road is equipped with venthole, and the venthole interlocks aperture in the boring aeration pipeline bilateral, aperture angle Degree is 45 ° obliquely of horizontal direction.

127. biomembrane reaction of high order equipment as claimed in claim 3, which is characterized in that the boring aeration pipe road is equipped with Venthole, the venthole interlock aperture in the boring aeration pipeline bilateral, and blowing angle is 45 ° obliquely of horizontal direction.

128. biomembrane reaction of high order equipment as claimed in claim 6, which is characterized in that the boring aeration pipe road is equipped with Venthole, the venthole interlock aperture in the boring aeration pipeline bilateral, and blowing angle is 45 ° obliquely of horizontal direction.

129. biomembrane reaction of high order equipment as claimed in claim 8, which is characterized in that the boring aeration pipe road is equipped with Venthole, the venthole interlock aperture in the boring aeration pipeline bilateral, and blowing angle is 45 ° obliquely of horizontal direction.

130. biomembrane reaction of high order equipment as claimed in claim 11, which is characterized in that the boring aeration pipe road is set Have a venthole, the venthole interlocks aperture in the boring aeration pipeline bilateral, blowing angle be horizontal direction obliquely 45°。

131. biomembrane reaction of high order equipment as claimed in claim 15, which is characterized in that the boring aeration pipe road is set Have a venthole, the venthole interlocks aperture in the boring aeration pipeline bilateral, blowing angle be horizontal direction obliquely 45°。

132. biomembrane reaction of high order equipment as claimed in claim 20, which is characterized in that the boring aeration pipe road is set Have a venthole, the venthole interlocks aperture in the boring aeration pipeline bilateral, blowing angle be horizontal direction obliquely 45°。

133. biomembrane reaction of high order equipment as claimed in claim 26, which is characterized in that the boring aeration pipe road is set Have a venthole, the venthole interlocks aperture in the boring aeration pipeline bilateral, blowing angle be horizontal direction obliquely 45°。

134. biomembrane reaction of high order equipment as claimed in claim 34, which is characterized in that the boring aeration pipe road is set Have a venthole, the venthole interlocks aperture in the boring aeration pipeline bilateral, blowing angle be horizontal direction obliquely 45°。

135. biomembrane reaction of high order equipment as claimed in claim 41, which is characterized in that the boring aeration pipe road is set Have a venthole, the venthole interlocks aperture in the boring aeration pipeline bilateral, blowing angle be horizontal direction obliquely 45°。

136. biomembrane reaction of high order equipment as claimed in claim 49, which is characterized in that the boring aeration pipe road is set Have a venthole, the venthole interlocks aperture in the boring aeration pipeline bilateral, blowing angle be horizontal direction obliquely 45°。

137. biomembrane reaction of high order equipment as claimed in claim 58, which is characterized in that the boring aeration pipe road is set Have a venthole, the venthole interlocks aperture in the boring aeration pipeline bilateral, blowing angle be horizontal direction obliquely 45°。

138. the biomembrane reaction of high order equipment as described in claim 67, which is characterized in that the boring aeration pipe road is set Have a venthole, the venthole interlocks aperture in the boring aeration pipeline bilateral, blowing angle be horizontal direction obliquely 45°。

139. the biomembrane reaction of high order equipment as described in claim 77, which is characterized in that the boring aeration pipe road is set Have a venthole, the venthole interlocks aperture in the boring aeration pipeline bilateral, blowing angle be horizontal direction obliquely 45°。

140. the biomembrane reaction of high order equipment as described in claim 88, which is characterized in that the boring aeration pipe road is set Have a venthole, the venthole interlocks aperture in the boring aeration pipeline bilateral, blowing angle be horizontal direction obliquely 45°。

The 141. biomembrane reaction of high order equipment as described in claim 100, which is characterized in that the boring aeration pipe road is set Have a venthole, the venthole interlocks aperture in the boring aeration pipeline bilateral, blowing angle be horizontal direction obliquely 45°。

The 142. biomembrane reaction of high order equipment as described in claim 113, which is characterized in that the boring aeration pipe road is set Have a venthole, the venthole interlocks aperture in the boring aeration pipeline bilateral, blowing angle be horizontal direction obliquely 45°。

143. such as claim 2,4-5,7,9-10,12-14,16-19,21-25,27-33,35-40,42-48,50-57,59- 66, biomembrane reaction of high order equipment described in one of 68-76,78-87,89-99,101-112,114-125,127-142, it is special Sign is that the height of the boring aeration pipeline is adjustable.

144. biomembrane reaction of high order equipment as claimed in claim 3, which is characterized in that the height of the boring aeration pipeline It is adjustable.

145. biomembrane reaction of high order equipment as claimed in claim 6, which is characterized in that the height of the boring aeration pipeline It is adjustable.

146. biomembrane reaction of high order equipment as claimed in claim 8, which is characterized in that the height of the boring aeration pipeline It is adjustable.

147. biomembrane reaction of high order equipment as claimed in claim 11, which is characterized in that the height of the boring aeration pipeline It spends adjustable.

148. biomembrane reaction of high order equipment as claimed in claim 15, which is characterized in that the height of the boring aeration pipeline It spends adjustable.

149. biomembrane reaction of high order equipment as claimed in claim 20, which is characterized in that the height of the boring aeration pipeline It spends adjustable.

150. biomembrane reaction of high order equipment as claimed in claim 26, which is characterized in that the height of the boring aeration pipeline It spends adjustable.

151. biomembrane reaction of high order equipment as claimed in claim 34, which is characterized in that the height of the boring aeration pipeline It spends adjustable.

152. biomembrane reaction of high order equipment as claimed in claim 41, which is characterized in that the height of the boring aeration pipeline It spends adjustable.

153. biomembrane reaction of high order equipment as claimed in claim 58, which is characterized in that the height of the boring aeration pipeline It spends adjustable.

The 154. biomembrane reaction of high order equipment as described in claim 67, which is characterized in that the height of the boring aeration pipeline It spends adjustable.

The 155. biomembrane reaction of high order equipment as described in claim 77, which is characterized in that the height of the boring aeration pipeline It spends adjustable.

The 156. biomembrane reaction of high order equipment as described in claim 88, which is characterized in that the height of the boring aeration pipeline It spends adjustable.

The 157. biomembrane reaction of high order equipment as described in claim 100, which is characterized in that the height of the boring aeration pipeline It spends adjustable.

The 158. biomembrane reaction of high order equipment as described in claim 113, which is characterized in that the height of the boring aeration pipeline It spends adjustable.

The 159. biomembrane reaction of high order equipment as described in claim 126, which is characterized in that the height of the boring aeration pipeline It spends adjustable.