CN211141851U

CN211141851U - Functional microorganism liquid culture synergistic reactor

Info

Publication number: CN211141851U
Application number: CN201922111056.5U
Authority: CN
Inventors: 蔡勤丰; 李传伟; 杨素伟; 林晓丹; 蔡建丰; 陈诗如
Original assignee: Shantou High New Shengtai Environmental Protection Biotechnology Co ltd
Current assignee: Shantou High New Shengtai Environmental Protection Biotechnology Co ltd
Priority date: 2019-11-30
Filing date: 2019-11-30
Publication date: 2020-07-31
Anticipated expiration: 2029-11-30

Abstract

A functional microorganism liquid culture synergistic reactor comprises a culture storage tank, biological fillers, a suspension mechanism, a water inlet pump, a gas distribution disc, an oxygen distribution device, a controller, a microorganism liquid ejector and a microorganism embedding module; the culture storage box is provided with a slow release bin, and the microorganism embedding module is arranged in the slow release bin; the microorganism liquid ejector comprises a high-pressure water pump, a water suction pipe, a water delivery pipe and a jet flow water pipe, wherein the outer end of the jet flow water pipe extends out of the side wall of the cultivation storage tank. Through addding microorganism liquid ejector and microorganism embedding module, release the functional microorganism of selecting in advance, form secondary function microorganism liquid and store in cultivating the storage tank, and the microorganism ejector is then with secondary microorganism liquid extraction and jet out to the silt top layer in peripheral waters, the quick infiltration of secondary function microorganism liquid of efflux output and post in submarine silt, carry out purification treatment on the spot to the sewage normal position, make the organic matter in the silt handle in addition, make silt restore to sandy soil.

Description

Functional microorganism liquid culture synergistic reactor

Technical Field

The utility model relates to a microorganism sewage treatment device especially relates to a function microorganism liquid culture increase effect reactor.

Background

The water environment is an important foundation of human living environment and ecological environment, and water resources become a scarce precious resource in the world at present. At present, most of cities and towns and rural areas in China are wide in area, and due to the reasons of planning lag, disordered pollution discharge, treatment deficiency and the like, the water environment quality is generally poor, so that the living environment of residents in the cities and towns and the rural areas is seriously influenced, and the body health of people is further influenced.

At present, in cities and towns and rural areas, sewage mainly comprises a large amount of domestic sewage, industrial sewage and livestock breeding wastewater, under the condition that independent and effective treatment is not carried out on a single sewage body at the present stage, a plurality of polluted mixed water areas are formed, and more serious damage is caused to water resources and water environment, so that the treatment and restoration difficulty of the water resources is increased, the existing sewage treatment technology generally comprises a physical method, a chemical method and a biological method, and the physical method and the chemical method have the problems of higher treatment cost, poorer treatment effect and persistence, easy secondary pollution and the like.

In order to solve the above problems, the applicant proposed and authorized a utility model on 19.01.2015, application number CN201510025033.6, entitled microbial flora mother liquor cultivation generator and a microbial sewage treatment method thereof, and disclosed a specific structure of microbial flora mother liquor cultivation generator, which comprises a microbial generation box, a biological filling bin, a biological filling material, a water inlet device, a slag discharge device, a water-gas synchronous cutting and distribution device and an automatic control device, wherein the water-gas synchronous cutting and distribution device comprises an oxygen increasing device, a water distribution box, a water supply pipe, an air supply pipe, a water-gas mixing bin and an air distribution plate, the air distribution plate is provided with a plurality of air outlets, the top wall of the water-gas mixing bin is provided with a jet orifice, and the top wall and the jet orifice of the water-gas mixing bin form a water-gas cutting plate. Water is supplied to the water-air mixing bin from top to bottom, the pressure difference is increased, gas and water are fully mixed in the water-air mixing bin, the water-air cutting disc uniformly cuts the water-air mixture, water and air are more uniformly mixed, and then the water and air are supplied to the biological filler from bottom to top, so that the dynamic contact effect of the water-air mixture and the biological filler is increased, the microbial activity is greatly improved, and more active microbial floras and more biomass can be cultivated.

The purification equipment manufactured according to the patent CN201510025033.6 has a prominent performance in sewage treatment, and has certain effect on the treatment of black and odorous water and bottom sludge, but the purification equipment is still not satisfactory.

However, at present, the vast urban and rural areas still have serious pollution of black and odorous water, which directly damages the living health conditions of the urban and rural areas, seriously affects the faces and images of the urban and rural areas and hinders the development of urban and rural economy and the ecological civilization construction process.

In water pollution treatment, particularly black and odorous water body treatment, water bottom sludge is used as a main component of endogenous pollution, and due to the fact that a pollutant tight migration exchange relationship exists between the sludge and the water body, a large amount of deposited oxygen-consuming substances, nitrogen and phosphorus nutrients, organic pollutants and the like in the sludge continuously and repeatedly permeate the water body, so that the water body pollution is increased inevitably, and the treatment difficulty of the polluted water body is increased inevitably. At present, still basically, stop on the treatment method of artifical excavation submarine silt, the artifical excavation clearance cost a large amount of manpower and materials of submarine silt, the silt of clearing up moreover is piled up in large tracts of land on the bank and also can't be handled with reasonable low-cost, more has the potential harm that causes secondary pollution.

With the continuous development of environmental biotechnology, bioremediation technology is relatively widely applied to production practice as a treatment technology with low investment, high benefit and convenient operation, but most of the current common methods for treating underwater sludge by using microorganisms are to spray a microorganism preparation into a bacterial solution to pollute the water surface or to manufacture particles to be thrown into a polluted water body, and the two methods have obvious defects: (1) the speed of free diffusion of microorganisms to the sludge at the water bottom is slow; (2) the biological consumption is very large; (3) the subsequent cultivation domestication and the synergistic function are lacked. Therefore, the existing bioremediation technologies such as spraying bacteria liquid and scattering granular bacteria have the defects of low efficiency and large consumption.

Disclosure of Invention

The to-be-solved technical problem of the utility model is to provide a function microorganism liquid culture increase effect reactor and submarine silt processing method. The technical scheme is as follows:

the utility model provides a function microorganism liquid culture increases effect reactor, including cultivating the bin, a plurality of biofilm carrier, suspension mechanism, the intake pump, the gas distribution dish, distribution device and controller, suspension mechanism installs on cultivating the bin, the intake pump is installed on cultivating the lateral wall of bin, the gas distribution dish is installed in the lower part of cultivating the bin, constitute aqueous vapor mixing storehouse between gas distribution dish and the cultivating the bin bottom, distribution device installs the top of cultivating the bin, distribution device's oxygen suppliment mouth is in aqueous vapor mixing storehouse, each biofilm carrier is filled in cultivating the bin, characterized by: the device also comprises a microorganism liquid ejector and a plurality of microorganism embedding modules; a slow release bin is arranged at the upper part or the top of the cultivation storage tank, and the water inlet pump is communicated with the slow release bin through a water inlet pipe; each microorganism embedding module is arranged in the slow release bin; the microorganism liquid ejector comprises a high-pressure water pump, a water suction pipe, a water delivery pipe and at least one jet water pipe, wherein the high-pressure water pump is arranged at the upper part of the cultivation storage box, the water suction pipe and the water delivery pipe are both put down along the upper part and the lower part and are arranged in the inner cavity of the cultivation storage box, the lower end of the water suction pipe is positioned above the air distribution disc, the upper end of the water suction pipe is connected with the water inlet of the high-pressure water pump, the upper end of the water delivery pipe is connected with the water outlet of the high-pressure water pump, each jet water pipe is arranged at the bottom of the cultivation storage box and is positioned above the air distribution disc, the inner end of each jet water pipe is connected together and is connected with the lower end of the water delivery pipe; the water inlet pump, the air distribution device and the microorganism liquid ejector are all electrically connected with the controller.

The functional microorganism liquid culture synergistic reactor has the working principle that: the water quantity and air quantity are regulated and controlled by the automatic controller, the water supply time period and the oxygen supply time period are regulated, the water inlet pump absorbs water from a sewage water area and sends the water into the slow release bin, the microorganism embedding module is flushed, the microorganism embedding module releases preselected functional microorganisms to form primary functional microorganism liquid, the primary functional microorganism liquid enters the culture storage bin below and starts to be filmed on suspended biological fillers, the air distribution device conveys oxygen into a water-air mixing bin at the bottom of the culture storage bin, the oxygen and the water are fully mixed and are sprayed to an area where the biological fillers are located from bottom to top through a spray opening on an air distribution plate, favorable conditions for culture and domestication of the functional microorganisms are artificially created, the functional bacteria of the primary functional microorganism liquid can be quickly attached to the biofilm of the biological fillers and enhance the efficiency to generate secondary functional microorganism liquid, meanwhile, through the optimization of the material of the biological filler, the in-situ indigenous microorganism strains are screened, the strains are propagated and domesticated on the biological membrane, in a water-gas two-phase flow field, the biological membrane on the biological filler falls off and forms indigenous excellent microorganism strain liquid, and the secondary functional microorganism strain liquid is also merged, so that the biomass of the microbes with excellent advantages is richer, the secondary functional microorganism strain liquid is extracted by starting a high-pressure water pump of the microorganism strain ejector and is ejected to a sewage water area around the culture storage tank through each jet water pipe, because the whole functional microorganism strain culture synergistic reactor is suspended in the sewage water area, the bottom of the reactor is close to the surface layer of the underwater sludge, and each jet water pipe is arranged at the bottom of the culture storage tank, the secondary functional microorganism strain liquid output by the high-pressure jet can quickly infiltrate and reside in the underwater sludge, the method can be used for quickly and efficiently carrying out nitration, denitrification reaction and degradation on organic matters, ammonia nitrogen, phosphorus and harmful substances in the sewage and the sludge, not only can carry out in-situ purification treatment on the sewage, but also can degrade and reduce the organic matters in the sludge into sandy soil.

As the preferred scheme of the utility model, the functional microorganism liquid culture synergistic reactor further comprises a water-gas two-phase flow field internal circulation device, wherein the water-gas two-phase flow field internal circulation device comprises a circulation well, a circulation water pump, an internal circulation water pipe and a circulation pipe frame provided with a plurality of water flow injection holes, and each water flow injection hole is arranged on the circulation pipe frame along the clockwise or anticlockwise direction; the circulating water well is arranged on the cultivation storage box and communicated with the inner cavity of the cultivation storage box, the circulating water pump is arranged in the circulating water inlet well, the circulating pipe frame is arranged in the inner cavity of the cultivation storage box and above the gas distribution disc, the upper end of the internal circulating water pipe is connected with the water outlet of the circulating water pump, and the lower end of the internal circulating water pipe is connected with the circulating pipe frame. The water flow (mixed with the gas sprayed by the gas distribution device) pumped by the circulating water pump from the lower part of the cultivation storage box enters the circulating pipe frame through the internal circulating pipe and is sprayed out from the water flow spraying holes on the circulating pipe frame to form a convoluted water flow, and the convoluted water flow and the gas sprayed by the gas distribution device form a flow field in which water and gas are mutually mixed, so that the activity of microorganisms in the biological filling bin is further increased, the cultivation efficiency of functional microorganisms and excellent in-situ indigenous microorganisms is improved, in addition, the biofilm on the biological filling material is continuously washed through repeated internal circulation, the concentration of liquid of secondary functional microorganisms is improved, the functional microorganisms with higher concentration can be sprayed out during jet flow, and the planting efficiency of the functional microorganisms on underwater silt is greatly improved.

As a further preferable scheme of the present invention, the circulation pipe frame comprises a first pipe and a second pipe, the first pipe and the second pipe are communicated and connected in the middle; one end of the first pipeline and two ends of the second pipeline are both closed, and the other end of the first pipeline is used as a connecting port of the internal circulation pipe. The circulating pipe frame is provided with a first pipeline and a second pipeline, the first pipeline and the second pipeline are in cross communication connection in the middle, and water flow sprayed by the water flow spraying holes in the circulating pipe frame can form stronger swirling water flow. It is further preferred that the first duct is cross-connected to the second duct. The first pipeline and the second pipeline are symmetrically arranged in a cross shape, and water flow sprayed by the water flow spraying holes on the circulating pipe support rotates clockwise or anticlockwise.

As a further preferred aspect of the present invention, the suspension mechanism is an annular buoyancy tank, and the annular buoyancy tank is installed in the upper periphery of the cultivation storage box.

As a further preferred scheme of the utility model, be equipped with in the annular flotation tank with outside communicating intake shaft, the intake pump is installed in the intake shaft.

As a further preferable aspect of the present invention, the circulation well is provided in the annular buoyancy tank.

As a preferred scheme of the utility model, the gas distribution device comprises a first oxygenation pump, a second oxygenation pump, a gas supply pipe and a gas distribution plate, and a plurality of gas outlets are arranged on the gas distribution plate; the first oxygenation pump and the second oxygenation pump are installed at the top of the cultivation storage box, the gas distribution plate is arranged in the water-gas mixing bin, and the gas supply pipe is arranged in the cultivation storage box along the up-down direction; the first oxygenation pump and the second oxygenation pump are respectively connected with the upper end of the air supply pipe, and the lower end of the air supply pipe is connected with the air distribution plate. The gas distribution device is arranged to comprise a first oxygenation pump and a second oxygenation pump, and the first oxygenation pump and the second oxygenation pump work in turn by control, so that the service lives of the first oxygenation pump and the second oxygenation pump are prolonged; when the first oxygenation pump and the second oxygenation pump are controlled to work in parallel, the air pressure of gas entering the bottom of the culture storage tank is greatly increased, the defect that the air outlet is frequently blocked is effectively overcome, the speed of spraying the water-gas mixture from the jet orifice of the water-gas cutting disc is increased, sediments on the biological filler above the culture storage tank are washed away, the biological filler is washed again, the membrane hanging propagation of microorganisms on the biological filler is facilitated, and the culture efficiency of microbial flora mother liquor is improved. The gas panel generally comprises an annular tube, a transverse tube and a plurality of longitudinal tubes; two ends of the transverse pipe are communicated and connected with the annular pipe; the two ends and the middle part of the longitudinal pipe are respectively communicated and connected with the annular pipe and the transverse pipe. The gas distribution disc is provided with annular pipes, and the transverse pipes and the longitudinal pipes are staggered vertically and horizontally, so that the gas outlet holes are arranged in a net shape, and the gas is uniformly delivered at multiple points under the cutting action of the gas distribution disc, and the water and gas are mixed more uniformly.

As the preferable proposal of the utility model, the functional microorganism liquid culture synergistic reactor also comprises an externally-hung aeration device, the externally-hung aeration device comprises a third oxygenation pump, an aeration longitudinal pipe, at least two aeration transverse pipes and at least two aeration discs, the third oxygenation pump is arranged at the top of the culture storage tank, the aeration longitudinal pipe is arranged in the inner cavity of the culture storage tank along the vertical putting down, the lower ends of the aeration longitudinal pipes are positioned above the gas distribution disc, the upper ends of the aeration longitudinal pipes are connected with a third oxygenation pump, all the aeration transverse pipes are arranged at the bottom of the culture storage tank and above the gas distribution disc, the inner ends of all the aeration transverse pipes are connected together and connected with the lower ends of the aeration longitudinal pipes, the outer ends of all the aeration transverse pipes extend out of the culture storage tank from the side wall of the culture storage tank, and all the aeration discs are arranged at the outer ends of the corresponding aeration transverse pipes. Through adding outer hanging aeration equipment, for cultivating the peripheral silt top layer oxygenation of polluting the water of bin, improve the activity of implanting functional microorganism and the native dominant microorganism of normal position, make the functional microorganism of implanting can be hosted fast in silt and breed, make the silt of functional microorganism handle can in lasting, normality.

As the utility model discloses further preferred scheme, the aeration dish includes roof and back taper casing, and the uncovered installation of back taper casing is on the lower surface of roof and sealing connection, and the back taper casing constitutes the gas receiver with the roof, and the lower extreme point portion of back taper casing is seted up with the communicating air inlet of air chamber, has seted up a plurality ofly on the back taper casing and the communicating aeration mouth of air chamber. The aeration port is arranged on the conical surface of the inverted cone-shaped shell, namely the aeration port is arranged downwards, so that oxygen can permeate into a sludge layer more easily, the activity of implanted functional microorganisms and in-situ indigenous dominant microorganisms is further improved, and meanwhile, the oxygen consumption requirement of the functional microorganisms on the organic matter degradation and nitrification process is more favorably met.

As a further preferred scheme of the utility model, it is a plurality of aeration openings divide into the multirow, and every row all has a plurality of aeration openings, and each row of aeration openings is all certainly the air inlet extends to the uncovered edge of back taper casing.

As the preferred scheme of the utility model, the slow release bin is arranged at the top of the cultivation storage box and comprises a bin body, an annular water tank, a pipeline frame and a plurality of water spray heads; the annular water tank is arranged at the top of the bin body, the bottom of the annular water tank is provided with a plurality of first water through holes communicated with the bin body, and the bottom of the bin body is provided with a second water through hole; the pipeline frame is arranged in the annular water tank, and each water spraying head is arranged on the pipeline frame; each microorganism embedding module is arranged in the annular bin body.

As a further preferred aspect of the present invention, the annular water tank includes a bottom plate, an outer annular wall, an inner annular wall and a top cover, each of the first water holes is disposed on the bottom plate, the lower ends of the outer annular wall and the inner annular wall are both disposed on the bottom plate, the inner annular wall is disposed in the outer annular wall, the top cover covers the upper ends of the outer annular wall and the inner annular wall, and the outer annular wall, the inner annular wall and the bottom plate form an annular groove.

As a further preferred scheme of the utility model, the pipeline frame includes ring conduit and many straight tubes, and the inner of each straight tube all communicates with each other with the ring conduit and is connected to each straight tube is all along the radial outer extension of ring conduit, and the outer end of one of them straight tube is as the water inlet, and the outer end of all the other each straight tubes is all sealed, each the sprinkler bead is all installed on corresponding straight tube.

As a still further preferred embodiment of the present invention, each of the water spraying directions of the water spraying heads has an included angle with the horizontal plane, and the spraying directions of the water spraying heads are deviated from the length direction of the straight pipe, and the directions of the water spraying heads are the same.

Compared with the prior art, the utility model, have following advantage:

the utility model discloses a gas distribution device sends oxygen into the aqueous vapor mixing bin of cultivation bin bottom, make aqueous vapor homogeneous mixing, spout in the biofilm carrier place region from bottom to top, increased aqueous vapor mixture and biofilm carrier dynamic contact effect, improved microbial activity, cultivate more vigorous, the microbial community that the biomass is more, improve sewage treatment effect by a wide margin, on this basis, microorganism liquid ejector and a plurality of microorganism embedding module have been add, wash microorganism embedding module through annular rivers, release preselected function microorganism, make function microorganism be attached to fast and breed and strengthen the increase on biofilm carrier's hanging membrane, finally form secondary function microorganism liquid and store in cultivation bin, and the microorganism ejector then will cultivate the secondary microorganism liquid extraction in the bin and jet out the silt top layer in peripheral waters, the secondary functional microorganism liquid output by the high-pressure jet flow can rapidly permeate and reside in underwater silt, and can rapidly and efficiently nitrify, denitrify and degrade organic matters, ammonia nitrogen, phosphorus and harmful substances of sewage and silt, so that the sewage in situ is purified in situ, and the organic matters in the silt are degraded and reduced into sandy soil, and the secondary functional microorganism liquid is continuously output in a circulating manner and forms a reciprocating circulating fixed potential, so that the functional microorganism liquid culture synergistic reactor can continuously and normally treat the sewage and the underwater silt, and the functional microorganism liquid culture synergistic reactor also can continuously and naturally diffuse and propagate in the process of outputting the high-pressure jet flow, so that the distribution of the functional microorganism in a silt layer at the underwater is wider, and the sludge treatment range is wider.

Drawings

FIG. 1 is a schematic structural view of a preferred embodiment of the present invention;

FIG. 2 is a schematic structural view of a gas panel;

FIG. 3 is a schematic structural view of a microorganism liquid ejector;

FIG. 4 is a schematic structural view of a slow release chamber with an annular water tank disposed on the chamber body;

FIG. 5 is a schematic view of the construction of the circulation tube holder;

fig. 6 is a schematic structural view of an aeration disc.

Detailed Description

The following further describes the preferred embodiments of the present invention with reference to the accompanying drawings.

As shown in fig. 1, the functional microorganism liquid culture synergistic reactor comprises a culture storage tank 1, a plurality of biological fillers 2, an annular buoyancy tank 3, a water inlet pump 4, an air distribution disc 5, an air distribution device 6, a controller (the controller and the culture storage tank 1 are arranged separately and are generally arranged on a shore, and are not shown in the figure), a water-gas two-phase flow field internal circulation device 8, a microorganism liquid ejector 9, a plurality of microorganism embedding modules 10 and an external hanging type aeration device 11; the annular floating box 3 is arranged on the upper periphery of the cultivation storage box 1, a water inlet well 12 communicated with the outside is arranged in the annular floating box 3, and the water inlet pump 4 is arranged in the water inlet well 12; the air distribution disc 5 is arranged at the lower part of the cultivation storage box 1, and a water-air mixing bin 13 is formed between the air distribution disc 5 and the bottom of the cultivation storage box 1; the top of the cultivation storage tank 1 is provided with a slow release bin 14, and the water inlet pump 4 is communicated with the slow release bin 14 through a water inlet pipe 15; the gas distribution device 6 comprises a first oxygenation pump 601, a second oxygenation pump 602, a gas supply pipe 603 and a gas distribution plate 604, and as shown in fig. 2, the gas distribution plate 604 is provided with a plurality of gas outlet holes 605; the first oxygenation pump 601 and the second oxygenation pump 602 are installed on the slow release bin 14 at the top of the cultivation storage tank 1, the gas distribution disc 604 is arranged in the water-gas mixing bin 13, and the gas supply pipe 603 is arranged in the cultivation storage tank 1 along the up-down direction; the first oxygenation pump 601 and the second oxygenation pump 602 are respectively connected with the upper end of an air supply pipe 603, and the lower end of the air supply pipe 603 is connected with an air distribution plate 604; the circulating device 8 in the water-gas two-phase flow field comprises a circulating water well 801, a circulating water pump 802, an internal circulating water pipe 803 and a circulating pipe frame 805 provided with a plurality of water flow injection holes 804, wherein the water flow injection holes 804 are arranged on the circulating pipe frame 805 along the clockwise direction or the anticlockwise direction; the circulating water well 801 is arranged in the annular buoyancy tank 3 and communicated with the inner cavity of the cultivation storage tank 1, the circulating water pump 802 is arranged in the circulating water inlet well 801, the circulating pipe frame 805 is arranged in the inner cavity of the cultivation storage tank 1 and above the gas distribution disc 5, the upper end of the internal circulating water pipe 803 is connected with the water outlet of the circulating water pump 802, and the lower end of the internal circulating water pipe 803 is connected with the circulating pipe frame 805; as shown in fig. 1 and 3, the microorganism liquid ejector 9 includes a high-pressure water pump 901, a water suction pipe 902, a water pipe 903 and a plurality of jet water pipes 904, the high-pressure water pump 901 is installed on the slow release bin 14 (the high-pressure water pump 901 is installed on the upper portion of the cultivation storage tank 1), the water suction pipe 902 and the water pipe 903 are both set down in the inner cavity of the cultivation storage tank 1, the lower end of the water suction pipe 902 is above the air distribution disk 5, the upper end of the water suction pipe 902 is connected with the water inlet of the high-pressure water pump 901, the upper end of the water pipe 903 is connected with the water outlet of the high-pressure water pump 901, each jet water pipe 904 is arranged at the bottom of the cultivation storage tank 1 and above the air distribution disk 5, the inner ends of each jet water pipe 904 are connected together and connected with the lower end of the water pipe 903, and the outer end of each jet water pipe 904 extends; as shown in fig. 1, the externally hung aeration device 11 comprises a third oxygenation pump 111, an aeration longitudinal pipe 112, a plurality of aeration transverse pipes 113 and a plurality of aeration discs 114, wherein the third oxygenation pump 111 is installed on the slow release bin 14 at the top of the culture storage tank 1, the aeration longitudinal pipe 112 is arranged in the inner cavity of the culture storage tank 1 along the up-down direction, the lower end of the aeration longitudinal pipe 112 is arranged above the gas distribution disc 5, the upper end of the aeration longitudinal pipe 112 is connected with the third oxygenation pump 111, each aeration transverse pipe 113 is arranged at the bottom of the culture storage tank 1 and above the gas distribution disc 5, the inner ends of each aeration transverse pipe 113 are connected together and connected with the lower end of the aeration longitudinal pipe 112, the outer end of each aeration transverse pipe 113 extends out from the side wall of the culture storage tank 1, and each aeration disc 114 is installed at the outer end of the corresponding aeration transverse pipe 113; each microorganism embedding module 10 is arranged in the slow release bin 14; each biological filler 2 is filled in the culture storage tank 1; the water inlet pump 4, the air distribution device 6, the water-gas two-phase flow field internal circulation device 8, the microorganism liquid ejector 9 and the externally hung aeration device 11 are all electrically connected with the controller.

The controller generally adopts a single chip microcomputer and related circuits, and can also adopt a microprocessor and related circuits.

As shown in fig. 4, the slow release chamber 14 includes a chamber body 141, an annular water tank 142, a pipe rack 143, and a plurality of water spray heads 144; an annular water tank 142 is mounted on the top of the bin body 141; the annular water tank 142 comprises a bottom plate 14201, an outer annular wall 14202, an inner annular wall 14203 and a top cover 14204, wherein the bottom plate 14201 is provided with a plurality of first water through holes 14205 communicated with the bin body 141; a plurality of second water through holes 146 are formed at the bottom of the bin body 1; the lower ends of the outer ring wall 14202 and the inner ring wall 14203 are both arranged on the bottom plate 14201, the inner ring wall 14203 is positioned in the outer ring wall 14202, the top cover 14204 covers the upper ends of the outer ring wall 14202 and the inner ring wall 14203, and the outer ring wall 14202, the inner ring wall 14203 and the bottom plate 14201 form an annular groove 147; the pipeline 143 rack is installed in the annular groove 147 of the annular water tank 142, the pipeline rack 143 includes an annular pipeline 14301 and a plurality of straight pipes 14302, the inner end of each straight pipe 14302 is connected with the annular pipeline 14301 in a communication manner, each straight pipe 14302 extends outwards along the radial direction of the annular pipeline 14301, the outer end of one straight pipe 14302 serves as a water inlet, the outer ends of the other straight pipes 14302 are closed, each water spraying head 144 is installed on the corresponding straight pipe 14302, the water spraying direction of each water spraying head 144 forms an included angle with the horizontal plane, the spraying direction of each water spraying head 144 deviates from the length direction of the straight pipe 14302, and the orientation of each water spraying head 144 is the same.

The microorganism embedding module 10 generally embeds and presses the preselected functional microorganism strains into blocks by using polyurethane as a carrier material, wherein the functional microorganism strains generally comprise bacillus, pediococcus acidilactici, acidovorous bacteria, acinetobacter, mycobacterium avium denitrificans, pediococcus pentosaceus, pichia pastoris and the like, and can be optimized or combined according to actual requirements.

The air distribution plate 5 may be a plate body or a partition plate, and the plate body or the partition plate is provided with a plurality of injection ports.

In this embodiment, the slow release chamber 14 is an independent box body, and the slow release chamber 14 is arranged at the top of the cultivation storage box 1; the slow release chamber 14 can also be formed by dividing the inner cavity of the cultivation storage box 1, a water leakage clapboard is arranged at the upper part of the inner cavity of the cultivation storage box 1, and the water leakage clapboard and the inner side wall at the upper part of the cultivation storage box 1 form the slow release chamber 14 together.

As shown in fig. 5, the circulation pipe support 805 includes a first pipe 8051 and a second pipe 8052, and the first pipe 8051 is connected to the second pipe 8052 in communication therewith; one end of the first pipe 8051 and both ends of the second pipe 8052 are closed, and the other end of the first pipe 8051 serves as a connection port with the inner circulation water pipe 803. The circulation pipe frame 805 is provided with a first pipe 8051 and a second pipe 8052, the first pipe 8051 and the second pipe 8052 are connected in a cross communication in the middle, and the water flow sprayed from the water flow spraying holes 804 on the circulation pipe frame 805 can form a stronger swirling water flow. It is further preferred that the first conduit 8051 is cross-connected to the second conduit 8052. The first pipe 8051 and the second pipe 8052 are symmetrically arranged in a cross shape, and the water flow ejected from the water flow ejection holes 804 of the circulation pipe support 805 is formed to revolve clockwise or counterclockwise.

In the slow release bin 14, external sewage is sprayed into the annular groove 147 of the annular water tank 142 through the water spray head 144 of the slow release bin 14, the microorganism embedding module 10 in the lower bin body 141 is washed, the microorganism embedding module 10 releases preselected functional microorganisms and forms primary functional microorganism liquid, the primary functional microorganism liquid flows out through the second water passing holes 146 on the bottom of the bin body 141, the subsequent oxygen increasing and film hanging manner can be used for enhancing the efficiency, and the output is used for treating a sludge layer of a polluted water body, namely, functional microorganism strains can be preselected by the microorganism embedding module 10 for cultivation, organic matters, ammonia nitrogen, phosphorus and harmful substances in the sewage and sludge are subjected to nitrification, denitrification reaction and degradation, and the sludge treatment is more targeted and efficient.

The annular water tank 142 is arranged at the top of the slow release bin 14, and water sprayed from the water spray head 144 repeatedly flows in the annular groove 147 to flush the microorganism embedding module 10, so that the efficiency of releasing functional microorganism strains by the microorganism embedding module 10 is higher.

The spraying direction of each water spraying head 144 is deviated from the length direction of the straight pipe 14302 and the direction is the same, so that the water sprayed from the water spraying heads 144 circularly flows in the circular groove 147 in a fixed direction to form a rotational flow, and the washing effect on the microorganism embedding module 10 is better.

As shown in fig. 6, the aeration disc 114 includes a top plate 1141 and an inverted cone housing 1142, an opening of the inverted cone housing 1142 is mounted on a lower surface of the top plate 1141 and is hermetically connected to the lower surface, the inverted cone housing 1142 and the top plate 1141 form an air storage chamber, a lower tip portion of the inverted cone housing 1142 is provided with an air inlet 1143 communicating with the air chamber, the inverted cone housing 1142 is provided with a plurality of aeration ports 1144 communicating with the air chamber, the aeration ports 1144 are divided into a plurality of rows, each row has a plurality of aeration ports 1144, and each row of aeration ports 1144 extends from the air inlet 1143 to an opening edge of the inverted cone housing 1142. The aeration ports 1144 are arranged on the conical surface of the inverted cone-shaped shell 1142, that is, the aeration ports 1144 are arranged downward, so that oxygen can easily permeate into a sludge layer, and the activity of the implanted functional microorganisms and the in-situ indigenous dominant microorganisms is further improved.

The functional microorganism liquid culture synergistic reactor has the working principle that: the water quantity and air quantity are regulated and controlled by the automatic controller, the water supply time period and the oxygen supply time period are regulated, the water is sucked from the sewage water area by the water inlet pump 4, the water is sent into the slow release bin 14 through the water spray head 144 at the top of the slow release bin 14, the microorganism embedding module 10 is washed, the microorganism embedding module 10 releases the preselected functional microorganisms and forms primary functional microorganism liquid, the primary functional microorganism liquid enters the culture storage bin 1 below and is attached and propagated on the hanging film of the biological filler 2, the air distribution device 6 sends oxygen into the water-air mixing bin 13 at the bottom of the culture storage bin 1, the oxygen and the water are fully mixed and are sprayed to the area where the biological filler 13 is located from bottom to top through the spray opening on the air distribution plate 5, the favorable condition for functional microorganism culture is created by manual domestication, and the functional bacteria of the primary functional microorganism liquid can be rapidly attached and enhanced in synergism on the hanging film of the biological filler 2, generating secondary function microorganism liquid, simultaneously, screening in-situ indigenous microorganism strains through the optimization of the material of the biological filler 2, propagating and domesticating on a biological membrane, in a water-gas two-phase flow field, the biological membrane on the biological filler 2 falls off and forms indigenous excellent microorganism strain liquid, and the indigenous excellent microorganism strain liquid is also merged into the secondary function microorganism strain liquid, so that the biomass of microorganisms with excellent advantages is richer, the secondary function microorganism strain liquid is extracted by the starting of a high-pressure water pump 901 of a microorganism strain ejector 9 and is ejected to a sewage water area around the culture storage tank 1 through various jet water pipes 904, because the functional microorganism strain culture synergistic reactor is suspended in the sewage water area, the bottom of the functional microorganism strain culture synergistic reactor is close to the surface layer of underwater sludge, and various jet water pipes 904 are arranged at the bottom of the culture storage tank 1, the secondary function microorganism strain liquid output by high-pressure jet can quickly permeate into and reside in the underwater sludge, the method can be used for quickly and efficiently carrying out nitration, denitrification reaction and degradation on organic matters, ammonia nitrogen, phosphorus and harmful substances in the sewage and the sludge, not only can carry out in-situ purification treatment on the sewage, but also can degrade and reduce the organic matters in the sludge into sandy soil.

In the water-gas two-phase flow field internal circulation device 8, water flow (mixed with gas sprayed by a gas distribution device, generally air) pumped by the circulating water pump 802 from the lower part of the cultivation storage tank 1 enters the circulation pipe frame 805 through the internal circulation pipe 803 and is sprayed out from the water flow spray holes 804 on the circulation pipe frame 805 to form a circular water flow, the water flow and the gas sprayed out from the gas distribution device 6 form a flow field with two-phase interaction of water and gas, the activity of microorganisms in the biological filling bin is further increased, the cultivation efficiency of functional microorganisms and excellent in-situ indigenous microorganisms is improved, in addition, the biofilm on the biological filling is continuously washed through repeated internal circulation, the concentration of secondary functional microorganism liquid is improved, the functional microorganisms with higher concentration can be sprayed out during jet flow, and the planting efficiency of the functional microorganisms is greatly improved.

The gas distribution device 6 comprises a first oxygenation pump and a second oxygenation pump, and the first oxygenation pump and the second oxygenation pump work in turn by control, so that the service lives of the first oxygenation pump and the second oxygenation pump are prolonged; when the first oxygenation pump and the second oxygenation pump are controlled to work simultaneously, the air pressure of gas entering the bottom of the culture storage tank is greatly increased, the defect that the air outlet is often blocked is effectively overcome, the speed of spraying the water-gas mixture from the jet orifice of the water-gas cutting disc is increased, sediments on the biological filler above the culture storage tank are washed away, the biological filler is washed again, the membrane hanging propagation of microorganisms on the biological filler is facilitated, and the culture efficiency of microbial flora seed liquid is improved. The gas panel generally comprises an annular tube, a transverse tube and a plurality of longitudinal tubes; two ends of the transverse pipe are communicated and connected with the annular pipe; the two ends and the middle part of the longitudinal pipe are respectively communicated and connected with the annular pipe and the transverse pipe. The air distribution disc is provided with annular pipes, and transverse pipes and longitudinal pipes which are staggered vertically and horizontally, so that the air outlet holes are arranged in a net shape, multiple points can uniformly supply air, and the water and air can be mixed more uniformly.

Through addding outer hanging aeration equipment, for cultivating the peripheral silt top layer oxygenation of polluting the water of bin, improve the activity of implanting functional microorganism and the native dominant microorganism of normal position, make the functional microorganism of implanting can be hosted fast and breed in silt, satisfy the oxygen consumption demand of functional microorganism to organic matter degradation nitration process, make the silt of functional microorganism handle can last, the normality.

In addition, it should be noted that the names of the parts and the like of the embodiments described in the present specification may be different, and all the equivalent or simple changes made according to the structure, the features and the principle of the present invention are included in the protection scope of the present invention. Various modifications, additions and substitutions may be made by those skilled in the art without departing from the scope of the invention as defined in the accompanying claims.

Claims

1. The utility model provides a function microorganism liquid culture increases effect reactor, including cultivating the bin, a plurality of biofilm carrier, suspension mechanism, the intake pump, the gas distribution dish, distribution device and controller, suspension mechanism installs on cultivating the bin, the intake pump is installed on cultivating the lateral wall of bin, the gas distribution dish is installed in the lower part of cultivating the bin, constitute aqueous vapor mixing storehouse between gas distribution dish and the cultivating the bin bottom, distribution device installs the top of cultivating the bin, distribution device's oxygen suppliment mouth is in aqueous vapor mixing storehouse, each biofilm carrier is filled in cultivating the bin, characterized by: the device also comprises a microorganism liquid ejector and a plurality of microorganism embedding modules; a slow release bin is arranged at the upper part or the top of the cultivation storage tank, and the water inlet pump is communicated with the slow release bin through a water inlet pipe; each microorganism embedding module is arranged in the slow release bin; the microorganism liquid ejector comprises a high-pressure water pump, a water suction pipe, a water delivery pipe and at least one jet water pipe, wherein the high-pressure water pump is arranged at the upper part of the cultivation storage box, the water suction pipe and the water delivery pipe are both put down along the upper part and the lower part and are arranged in the inner cavity of the cultivation storage box, the lower end of the water suction pipe is positioned above the air distribution disc, the upper end of the water suction pipe is connected with the water inlet of the high-pressure water pump, the upper end of the water delivery pipe is connected with the water outlet of the high-pressure water pump, each jet water pipe is arranged at the bottom of the cultivation storage box and is positioned above the air distribution disc, the inner end of each jet water pipe is connected together and is connected with the lower end of the water delivery pipe; the water inlet pump, the air distribution device and the microorganism liquid ejector are all electrically connected with the controller.

2. The functional microorganism liquid culture synergistic reactor of claim 1, which is characterized in that: the functional microorganism liquid culture synergistic reactor also comprises a water-gas two-phase flow field internal circulating device, wherein the water-gas two-phase flow field internal circulating device comprises a circulating water well, a circulating water pump, an internal circulating water pipe and a circulating pipe frame provided with a plurality of water flow jet holes, and the water flow jet holes are arranged on the circulating pipe frame along the clockwise direction or the anticlockwise direction; the circulating water well is arranged on the cultivation storage box and communicated with the inner cavity of the cultivation storage box, the circulating water pump is arranged in the circulating water inlet well, the circulating pipe frame is arranged in the inner cavity of the cultivation storage box and above the gas distribution disc, the upper end of the internal circulating water pipe is connected with the water outlet of the circulating water pump, and the lower end of the internal circulating water pipe is connected with the circulating pipe frame.

3. The functional microorganism liquid culture synergistic reactor of claim 2, which is characterized in that: the circulating pipe frame comprises a first pipeline and a second pipeline, and the first pipeline is communicated and connected with the second pipeline in the middle; one end of the first pipeline and two ends of the second pipeline are both closed, and the other end of the first pipeline is used as a connector of the internal circulation water pipe.

4. The functional microorganism liquid culture synergistic reactor of claim 1, which is characterized in that: the functional microorganism liquid culture synergistic reactor further comprises an externally-mounted aeration device, the externally-mounted aeration device comprises a third oxygenation pump, an aeration longitudinal pipe, at least two aeration transverse pipes and at least two aeration discs, the third oxygenation pump is mounted at the top of the culture storage tank, the aeration longitudinal pipe is placed in an inner cavity of the culture storage tank along the vertical direction, the lower end of the aeration longitudinal pipe is located above the air distribution disc, the upper end of the aeration longitudinal pipe is connected with the third oxygenation pump, each aeration transverse pipe is arranged at the bottom of the culture storage tank and above the air distribution disc, the inner ends of the aeration transverse pipes are connected together and connected with the lower end of the aeration longitudinal pipe, the outer end of each aeration transverse pipe extends out of the culture storage tank from the side wall of the culture storage tank, and each aeration disc is mounted at the outer end of the corresponding aeration transverse pipe.

5. The functional microorganism liquid culture synergistic reactor of claim 4, which is characterized in that: the aeration dish includes roof and back taper casing, and the uncovered of back taper casing is installed on the lower surface of roof and sealing connection, and back taper casing constitutes the gas receiver with the roof, and the lower extreme point portion of back taper casing is seted up with the communicating air inlet of air chamber, has seted up a plurality ofly on the back taper casing and the communicating aeration mouth of air chamber.

6. The functional microorganism liquid culture synergistic reactor of claim 1, which is characterized in that: the slow release bin is arranged at the top of the cultivation storage box and comprises a bin body, an annular water tank, a pipeline frame and a plurality of water spray heads; the annular water tank is arranged at the top of the bin body, the bottom of the annular water tank is provided with a plurality of first water through holes communicated with the bin body, and the bottom of the bin body is provided with a second water through hole; the pipeline frame is arranged in the annular water tank, and each water spraying head is arranged on the pipeline frame; each microorganism embedding module is arranged in the annular bin body.

7. The functional microorganism liquid culture synergistic reactor of claim 6, which is characterized in that: the annular water tank comprises a bottom plate, an outer annular wall, an inner annular wall and a top cover, wherein each first water passing hole is formed in the bottom plate, the lower ends of the outer annular wall and the inner annular wall are arranged on the bottom plate, the inner annular wall is located in the outer annular wall, the top cover covers the upper ends of the outer annular wall and the inner annular wall, and the outer annular wall, the inner annular wall and the bottom plate form an annular groove.

8. The functional microorganism liquid culture synergistic reactor of claim 7, which is characterized in that: the pipeline frame comprises an annular pipeline and a plurality of straight pipes, the inner end of each straight pipe is communicated and connected with the annular pipeline, each straight pipe extends outwards along the radial direction of the annular pipeline, the outer end of one straight pipe serves as a water inlet, the outer ends of the other straight pipes are sealed, and each water spraying head is arranged on the corresponding straight pipe; the water spraying direction of each water spraying head forms an included angle with the horizontal plane, the spraying direction of each water spraying head deviates from the length direction of the straight pipe, and the orientation of each water spraying head is the same.