CN104986864A - Bacterial-algal symbiotic reactor - Google Patents
Bacterial-algal symbiotic reactor Download PDFInfo
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- CN104986864A CN104986864A CN201510400540.3A CN201510400540A CN104986864A CN 104986864 A CN104986864 A CN 104986864A CN 201510400540 A CN201510400540 A CN 201510400540A CN 104986864 A CN104986864 A CN 104986864A
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- reactor
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- pipe connecting
- helotism
- unitary reactor
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 13
- 239000010865 sewage Substances 0.000 claims description 30
- 239000004744 fabric Substances 0.000 claims description 14
- 241000195493 Cryptophyta Species 0.000 claims description 13
- 241000894006 Bacteria Species 0.000 claims description 10
- 239000000126 substance Substances 0.000 claims description 9
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 8
- 230000000050 nutritive effect Effects 0.000 claims description 7
- 238000011144 upstream manufacturing Methods 0.000 claims description 6
- 239000012530 fluid Substances 0.000 claims description 4
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 3
- 239000001569 carbon dioxide Substances 0.000 claims description 3
- 230000007423 decrease Effects 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims description 3
- 238000000746 purification Methods 0.000 abstract description 7
- 239000010802 sludge Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 6
- 230000029553 photosynthesis Effects 0.000 description 4
- 238000010672 photosynthesis Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 3
- 238000005286 illumination Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 235000011089 carbon dioxide Nutrition 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 241001148470 aerobic bacillus Species 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000009395 breeding Methods 0.000 description 1
- 230000001488 breeding effect Effects 0.000 description 1
- 230000019522 cellular metabolic process Effects 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 238000003306 harvesting Methods 0.000 description 1
- 230000008595 infiltration Effects 0.000 description 1
- 238000001764 infiltration Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 235000008935 nutritious Nutrition 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 230000000243 photosynthetic effect Effects 0.000 description 1
- 230000035790 physiological processes and functions Effects 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 238000002834 transmittance Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The invention discloses a bacterial-algal symbiotic reactor. The bacterial-algal symbiotic reactor comprises a connecting pipe and a plurality of unit reactors, wherein each unit reactor comprises a unit reactor inlet and a unit reactor outlet, the connecting pipe comprises a connecting pipe inlet and a connecting pipe outlet, the height from the connecting pipe inlet to the connecting pipe outlet is reduced gradually, each unit reactor inlet is communicated with a first port of the connecting pipe, each unit reactor outlet is communicated with a second port of the connecting pipe, the second port of the connecting pipe is located at the downstream in the water flow direction of the first port of the connecting pipe, and from the unit reactor located at the highest position to the unit reactor located at the lowest position, the heights of the unit reactors are reduced gradually. The bacterial-algal symbiotic reactor can better fit into the surrounding community environment, and the purification of polluted water inside a city is achieved by use of a bacterial-algal symbiotic system.
Description
[technical field]
The present invention relates to a kind of helotism reactor.
[background technology]
Traditional wastewater treatment plant is separated with city, builds in exurb more, and sewage long distance delivery causes construction cost high, and may because infiltration and leakage effects cause environmental pollution.The water treatment system that can be distributed in city is the future trend of urban water plant design.For realizing the successful construction of urban inner sewage purification system, the shortcoming that traditional wastewater treatment plant must overcome that floor space is large, outdoor, smell is dispersed etc.Meanwhile, traditional sewage purification process is mainly with centered by active sludge, but the resources such as nitrogen a large amount of in sewage, phosphorus can not make full use of by active sludge well; And the breath malodor of mud, be difficult to the psychology accreditation obtaining resident in city space.Adopt biotechnology, use the syntaxial system of bacterium and micro-algae to purify sewage, in conjunction with the water technology that other are complementary, traditional active sludge sewage purification method can be replaced.
Algae-bacteria symbiotic system (algal-bacterial symbiotic system) utilizes the physiological function between algea and bacteria two class biology to act synergistically the Freshwater ecosystems of purifying waste water.Phycophyta utilizes the CO in water by photosynthesis
2and NH
4 +, PO
4 3-deng nutritive substance, synthesis own cells material also discharges O
2; Aerobic bacteria then utilizes O in water
2organic pollutant is decomposed, transforms, produce CO
2with above-mentioned nutritive substance, to maintain the growth and breeding of algae, so move in circles, realize the biological purification of sewage.The efficiency that algae-bacteria symbiotic system is disposed of sewage depends on the many factors such as solar radiation amount, temperature, pollution level (load and toxicity) and the residence time.
Active sludge (activesludge) is the general name of microbial population and their organic substances of depending on and inorganic substance; within 1912, found by the Clarke (Clark) of Britain and Gage (Gage); active sludge can be divided into aerobic activated sludge and anaerobic grain active sludge, and active sludge is mainly used to process stain disease.Activated sludge process is a class Aerobic treatment method of the microorganism flco process organic sewage utilizing suspension growth.
Micro-algae be a class on land, ocean is widely distributed, the holophyte that nutritious, photosynthetic availability is high, polysaccharide, protein, pigment etc. that cellular metabolism produces, make it have good DEVELOPMENT PROSPECT in fields such as food, medicine, genetically engineered, liquid fuels.Algae Individual Size great disparity, wherein, only has the small algae monoid could differentiating its form to be under the microscope called micro-algae (microalgae) by people, so micro-algae is not the title on a taxonomy.
[summary of the invention]
More perfect in order to make to utilize helotism to process sewage, the invention provides a kind of helotism reactor.
A kind of helotism reactor, comprise pipe connecting and multiple unitary reactor, described unitary reactor comprises unitary reactor entrance and unitary reactor outlet, described pipe connecting comprises pipe connecting entrance and pipe connecting outlet, the height exporting described pipe connecting to described pipe connecting from described pipe connecting entrance reduces gradually, described unitary reactor entrance is communicated with the first interface of described pipe connecting, second orifice of described unitary reactor outlet and described pipe connecting, second interface of described pipe connecting is in the downstream of the water (flow) direction of the first interface of described pipe connecting, from being positioned at the unitary reactor of extreme higher position to the unitary reactor being positioned at extreme lower position, the height of unitary reactor reduces gradually.
In one embodiment, from being positioned at the unitary reactor of extreme higher position to the unitary reactor being positioned at extreme lower position, unitary reactor is round setting point spiral decline gradually, the projection in the horizontal plane of upper unitary reactor with under unitary reactor projection in the horizontal plane mutually stagger, the projection in the horizontal plane of upper unitary reactor than under unitary reactor projection in the horizontal plane closer to the distance of described setting point.
In one embodiment, export from described pipe connecting entrance to described pipe connecting, described pipe connecting reduces along unitary reactor gradually near described setting point side spiral.
In one embodiment, also comprise outside pipe connecting, multiple unitary reactor comprises adjacent first module reactor and second unit reactor, height residing for described first module reactor is greater than the height residing for described second unit reactor, the entrance of described first module reactor and the outlet of second unit reactor respectively with first interface and second orifice of described pipe connecting, the outlet of described first module reactor is communicated with by described outside pipe connecting with the entrance of second unit reactor.
In one embodiment, described pipe connecting is provided with the first valve in first interface upstream, the second valve is established in the upstream of the second interface of described pipe connecting, the 3rd valve is provided with between the entrance of described first module reactor and first interface, be provided with the 4th valve between the outlet of described second unit reactor and the second interface, between the outlet of described first module reactor and the entrance of second unit reactor, be provided with the 5th valve.
In one embodiment, be provided with in described unitary reactor whipping appts for stirring described unitary reactor fluid flow inside and/or,
The sub-body of described unitary reactor and upper body are respectively space that sewage occupies and the space that gas occupies, multiple sensors is provided with, for obtaining corresponding data message and sending to the master control system of helotism reactor in described unitary reactor.
In one embodiment, also comprise motor, connecting strand and multiple screen cloth for fixing bacterium algae, described multiple screen cloth is fixed on described connecting strand, described connecting strand is connected to the output terminal of described motor, described screen cloth and connecting strand are arranged in described unitary reactor, described motor for drive described multiple screen cloth near or away from the side of described unitary reactor.
In one embodiment, also comprise supply routine, described supply routine is used for transport of carbon dioxide in described unitary reactor and/or the nutritive substance for helotism.
In one embodiment, the top of described unitary reactor and side are transparent.
In one embodiment, also comprise the light-emitting device for carrying out light filling to unitary reactor, described light-emitting device is arranged between adjacent unitary reactor.
Each unitary reactor can work independently, and when some unitary reactors break down, need to safeguard, do not affect the work of other unitary reactors, therefore whole helotism reactor can continuous firing.
In certain embodiments, helotism reactor, because its construct pattern vertically extended, the spatial design closed, apparatus design is carried out for realizing bacterium frond system healthy and rapid development, Peripheral region environment can be incorporated better, realize at urban inner by helotism system dirty water purification.
In certain embodiments, the body structure that helotism reactor is closed, can avoid the diffusion of sewage peculiar smell.The structural form that top-down helical extends, meets water body kinetics, helps sewage to flow downward; Save and take up an area space; Handsome in appearance, be more convenient for incorporating space, community in urban areas.Corollary apparatus (agitator, light filling pipe, sensor) reasonable in design, can help helotism system health growth in casing, realize the fast purification of water body.
[accompanying drawing explanation]
Fig. 1 is the helotism reactor schematic top plan view of an embodiment of the present invention;
Fig. 2 is the schematic perspective view of the helotism reactor of an embodiment of the present invention;
Fig. 3 is the helotism reactor schematic top plan view of an embodiment of the present invention;
Fig. 4 is the helotism reactor schematic side view of an embodiment of the present invention;
Fig. 5 is the schematic diagram of the unitary reactor of the helotism reactor of an embodiment of the present invention;
Fig. 6 is the schematic side view of the unitary reactor of the helotism reactor of an embodiment of the present invention;
Fig. 7 is the cross-sectional schematic of the unitary reactor of the helotism reactor of an embodiment of the present invention.
[embodiment]
Below the preferred embodiment of invention is described in further detail.
As shown in Fig. 1 to 7, a kind of helotism reactor of embodiment, comprise pipe connecting 1 and multiple unitary reactor 17, 18, the size of each unitary reactor 17 can be the same or different, unitary reactor 17, 18 comprise unitary reactor entrance and unitary reactor outlet, pipe connecting 1 comprises pipe connecting entrance 15 and pipe connecting outlet 16, from being positioned at the unitary reactor of extreme higher position to the unitary reactor being positioned at extreme lower position, the height of unitary reactor reduces gradually, composition graphs 2 and 4 can be found out, the height of unitary reactor declines gradually, height as the aspect ratio unitary reactor 18 of unitary reactor 17 is large, the height exporting 16 pipe connectings 1 from pipe connecting entrance 15 to pipe connecting reduces gradually, composition graphs 1, 2 and 4, pipe connecting entrance 15 is positioned at the unitary reactor side of extreme higher position, and pipe connecting outlet 16 is positioned at the unitary reactor side of extreme lower position, unitary reactor entrance is communicated with the first interface of pipe connecting 1, second orifice of unitary reactor outlet and pipe connecting 1, second interface of pipe connecting 1 is in the downstream of the water (flow) direction of the first interface of pipe connecting 1.
When needing processed sewage to flow into from pipe connecting entrance 15, sewage enters unitary reactor from the first interface of pipe connecting 1, unitary reactor entrance, then sewage stops in unitary reactor, helotism, decomposes some nutritive substance in sewage.After sewage is necessarily processed, then flow out from unitary reactor outlet, flow out from the second interface of pipe connecting 1, and export 16 outflows along pipe connecting 1 from pipe connecting.Each unitary reactor can work independently, and when some unitary reactors break down, need to safeguard, do not affect the work of other unitary reactors, therefore whole helotism reactor can continuous firing.
Second orifice of unitary reactor outlet and pipe connecting 1, the mode that can adopt similar outside pipe connecting 13 directly with the second orifice, also successively through outside pipe connecting 13 and unitary reactor and the second orifice, the work object of helotism reactor can all can be realized.
In a more excellent embodiment, as shown in Figures 1 to 4, from being positioned at the unitary reactor of extreme higher position to the unitary reactor being positioned at extreme lower position, unitary reactor is round setting point spiral decline gradually, the projection in the horizontal plane of upper unitary reactor with under unitary reactor projection in the horizontal plane mutually stagger, with ensure under unitary reactor can receive comparatively sufficient sunlight, to ensure carrying out smoothly of algae photosynthesis, in height the projection in the horizontal plane of upper unitary reactor than under unitary reactor projection in the horizontal plane closer to the distance of setting point.In the present embodiment, all unitary reactors projection approximation in the horizontal plane forms a spiral of Archimedes, and the height as the aspect ratio unitary reactor 18 of unitary reactor 17 is large, and unitary reactor 17 is closer to the initial point of spiral of Archimedes.
In one embodiment, from pipe connecting entrance 15 to pipe connecting outlet 16, pipe connecting 1 reduces along unitary reactor gradually near setting point side spiral, compares pipe connecting 1 and is arranged on away from unitary reactor near setting point side, and such is arranged so that the length of pipe connecting 1 is shorter.
In one embodiment, also comprise outside pipe connecting 13, multiple unitary reactor comprises adjacent first module reactor 17 and second unit reactor 18, height residing for first module reactor 17 is greater than the height residing for second unit reactor 18, the entrance of first module reactor 17 and the outlet of second unit reactor 18 respectively with first interface and second orifice of pipe connecting 1, the outlet of first module reactor 17 is communicated with by outside pipe connecting 13 with the entrance of second unit reactor 18.Compared to the second orifice directly adopting outside pipe connecting 13 with pipe connecting 1, the present embodiment can save the length of outside pipe connecting 13.
In one embodiment, pipe connecting 1 is provided with the first valve 2 in first interface upstream, the second valve 3 is established in the upstream of the second interface of pipe connecting 1, the 3rd valve 4 is provided with between the entrance of first module reactor 17 and first interface, the 4th valve is provided with between the outlet of second unit reactor 18 and the second interface, the 5th valve 14 is provided with between the outlet of first module reactor 17 and the entrance of second unit reactor 18, preferably, the 5th valve 14 is arranged on the exit of first module reactor 17.
In one embodiment, in unitary reactor, being provided with the whipping appts for stirring unitary reactor fluid flow inside, depositing to prevent bacterium algae.
Helotism reactor can also comprise motor 7, connecting strand 9 and multiple screen cloth 8 for fixing bacterium algae, multiple screen cloth 8 is fixed on connecting strand 9, connecting strand 9 is connected to the output terminal of motor 7, screen cloth 8 and connecting strand 9 are arranged in each unitary reactor, 7 motors for drive multiple screen cloth 9 near or away from the side of unitary reactor, thus bacterium algae to be gathered in.
In one embodiment, helotism reactor also comprises supply routine, and supply routine is used for transport of carbon dioxide in unitary reactor and/or the nutritive substance for helotism.Supply routine can comprise the supply routine trunk 5 be positioned at outside unitary reactor and the supply routine side shoot 6 stretching into unitary reactor inside, like this to carry out the supply of carbonic acid gas and nutritive substance more efficiently, is beneficial to helotism.
In one embodiment, the top of unitary reactor and side are transparent, and sunlight is shining in unitary reactor, thus are beneficial to the photosynthesis of algae.
In one embodiment, after sewage enters unitary reactor, sewage only occupies the sub-body of unitary reactor, and namely unitary reactor top is the gas space, and sub-body is the fluid space that sewage occupies; Unitary reactor inside is provided with sensor, PH, temperature, illumination, transmittance etc. in detected gas and liquid environment, the data message obtained by wireless network transmissions to the master control system of helotism reactor, to realize the monitoring of master control system to each unitary reactor.
Helotism reactor can also comprise the light-emitting device for carrying out light filling to unitary reactor, light-emitting device is arranged between adjacent unitary reactor and (can irradiates the unitary reactor of both sides like this, can maximum using illumination), when illumination deficiency, light-emitting device can be utilized to carry out light filling, to promote the photosynthesis of algae.
During work, sewage enters from pipe connecting entrance 15, for the first module reactor 17 and the second reactor 18 that are positioned at extreme higher position, open the first valve 2, second valve 4, two the 5th valves 14, close the 4th valve in the 3rd valve 3 and second unit reactor 18 exit, sewage flows into first module reactor 17 and second unit reactor 18, when the sewage of second unit reactor 18 is close to time enough, close the 5th valve 14, when the 5th valve 14 is positioned at first module reactor 17 exit, sewage in the pipe connecting 13 of outside enters second unit reactor 18 completely, outside pipe connecting 13 can not be rested on, otherwise sewage herein effectively cannot carry out helotism reaction.
Then, again for next adjacent group unitary reactor (corresponding first module reactor 17 and second unit reactor 18), open the second valve 3, close the first valve 2 ... enter in next group unitary reactor smoothly, until enter enough sewage in the unitary reactor of left and right to make sewage.
Sewage in unitary reactor carries out the helotism reaction setting duration, in unitary reactor, relevant wireless senser can be set, can detect in real time parameters such as temperature, oxygen (solubilised state and gaseous state), carbonic acid gas (solubilised state and gaseous state), pH, can according to these parameters, carry out adjustment to unitary reactor in real time to control, such as, carry out relevant supply by supply routine, control the irradiation etc. of light compensating apparatus.Be arranged on the whipping appts bottom unitary reactor, necessary hydraulic disturbance can be provided, prevent frond from precipitating.Reactor head side can arrange negative suction system, can balance internal differential pressure and reduce stink.
When screen cloth 8 attached to enough bacterium algaes, in screen cloth 8 scrolling to unitary reactor more than liquid level, and then under the drive of the connecting strand 9 pulled at electric motor 7, concentrating inside unitary reactor, thus carrying out harvesting bacterium algae.
Above content is in conjunction with concrete preferred implementation further description made for the present invention, can not assert that specific embodiment of the invention is confined to these explanations.For general technical staff of the technical field of the invention, without departing from the inventive concept of the premise, some simple deduction or replace can also be made, all should be considered as belonging to the scope of patent protection that the present invention is determined by submitted to claims.
Claims (10)
1. a helotism reactor, comprise pipe connecting and multiple unitary reactor, it is characterized in that: described unitary reactor comprises unitary reactor entrance and unitary reactor outlet, described pipe connecting comprises pipe connecting entrance and pipe connecting outlet, the height exporting described pipe connecting to described pipe connecting from described pipe connecting entrance reduces gradually, described unitary reactor entrance is communicated with the first interface of described pipe connecting, second orifice of described unitary reactor outlet and described pipe connecting, second interface of described pipe connecting is in the downstream of the water (flow) direction of the first interface of described pipe connecting, from being positioned at the unitary reactor of extreme higher position to the unitary reactor being positioned at extreme lower position, the height of unitary reactor reduces gradually.
2. helotism reactor as claimed in claim 1, it is characterized in that: from being positioned at the unitary reactor of extreme higher position to the unitary reactor being positioned at extreme lower position, unitary reactor is round setting point spiral decline gradually, the projection in the horizontal plane of upper unitary reactor with under unitary reactor projection in the horizontal plane mutually stagger, the projection in the horizontal plane of upper unitary reactor than under unitary reactor projection in the horizontal plane closer to the distance of described setting point.
3. helotism reactor as claimed in claim 2, it is characterized in that: export from described pipe connecting entrance to described pipe connecting, described pipe connecting reduces along unitary reactor gradually near described setting point side spiral.
4. helotism reactor as claimed in claim 3, it is characterized in that: also comprise outside pipe connecting, multiple unitary reactor comprises adjacent first module reactor and second unit reactor, height residing for described first module reactor is greater than the height residing for described second unit reactor, the entrance of described first module reactor and the outlet of second unit reactor respectively with first interface and second orifice of described pipe connecting, the outlet of described first module reactor is communicated with by described outside pipe connecting with the entrance of second unit reactor.
5. helotism reactor as claimed in claim 4, it is characterized in that: described pipe connecting is provided with the first valve in first interface upstream, the second valve is established in the upstream of the second interface of described pipe connecting, the 3rd valve is provided with between the entrance of described first module reactor and first interface, be provided with the 4th valve between the outlet of described second unit reactor and the second interface, between the outlet of described first module reactor and the entrance of second unit reactor, be provided with the 5th valve.
6. helotism reactor as claimed in claim 4, is characterized in that: be provided with in described unitary reactor whipping appts for stirring described unitary reactor fluid flow inside and/or,
The sub-body of described unitary reactor and upper body are respectively space that sewage occupies and the space that gas occupies, multiple sensors is provided with, for obtaining corresponding data message and sending to the master control system of helotism reactor in described unitary reactor.
7. helotism reactor as claimed in claim 4, it is characterized in that: also comprise motor, connecting strand and multiple screen cloth for fixing bacterium algae, described multiple screen cloth is fixed on described connecting strand, described connecting strand is connected to the output terminal of described motor, described screen cloth and connecting strand are arranged in described unitary reactor, described motor for drive described multiple screen cloth near or away from the side of described unitary reactor.
8. helotism reactor as claimed in claim 4, is characterized in that: also comprise supply routine, and described supply routine is used for transport of carbon dioxide in described unitary reactor and/or the nutritive substance for helotism.
9. helotism reactor as claimed in claim 4, is characterized in that: the top of described unitary reactor and side are transparent.
10. helotism reactor as claimed in claim 4, is characterized in that: also comprise the light-emitting device for carrying out light filling to unitary reactor, described light-emitting device is arranged between adjacent unitary reactor.
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| CN109553197A (en) * | 2018-08-16 | 2019-04-02 | 吉林建筑大学 | A kind of bacteria and algae membrane reactor parameter acquisition system |
| CN116040809A (en) * | 2023-02-15 | 2023-05-02 | 杭州嘉澍环境监测有限公司 | Algae fungus sewage treatment plant |
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| CN104986864B (en) | 2017-01-25 |
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