CN115215427B - Hydraulic spin biological membrane purification system for small micro water body and working method - Google Patents
Hydraulic spin biological membrane purification system for small micro water body and working method Download PDFInfo
- Publication number
- CN115215427B CN115215427B CN202210937440.4A CN202210937440A CN115215427B CN 115215427 B CN115215427 B CN 115215427B CN 202210937440 A CN202210937440 A CN 202210937440A CN 115215427 B CN115215427 B CN 115215427B
- Authority
- CN
- China
- Prior art keywords
- fixedly connected
- water
- module
- shaft
- spinning device
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 91
- 238000000034 method Methods 0.000 title claims abstract description 19
- 238000000746 purification Methods 0.000 title claims description 15
- 239000012528 membrane Substances 0.000 title claims description 11
- 230000007246 mechanism Effects 0.000 claims abstract description 48
- 238000009987 spinning Methods 0.000 claims abstract description 46
- 239000000945 filler Substances 0.000 claims abstract description 34
- 230000005540 biological transmission Effects 0.000 claims abstract description 16
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 15
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 15
- VMHLLURERBWHNL-UHFFFAOYSA-M Sodium acetate Chemical compound [Na+].CC([O-])=O VMHLLURERBWHNL-UHFFFAOYSA-M 0.000 claims description 11
- 235000017281 sodium acetate Nutrition 0.000 claims description 11
- 239000001632 sodium acetate Substances 0.000 claims description 11
- 239000000463 material Substances 0.000 claims description 7
- 230000003647 oxidation Effects 0.000 claims description 6
- 238000007254 oxidation reaction Methods 0.000 claims description 6
- 238000010248 power generation Methods 0.000 claims description 5
- 210000002500 microbody Anatomy 0.000 claims description 4
- 238000012856 packing Methods 0.000 claims description 4
- 238000006243 chemical reaction Methods 0.000 claims description 3
- 230000005484 gravity Effects 0.000 claims description 3
- 230000000149 penetrating effect Effects 0.000 claims description 3
- 238000003860 storage Methods 0.000 claims description 3
- 230000009471 action Effects 0.000 claims description 2
- 238000011049 filling Methods 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 24
- 229910052799 carbon Inorganic materials 0.000 abstract description 24
- 230000000694 effects Effects 0.000 abstract description 13
- 230000033001 locomotion Effects 0.000 abstract description 11
- 230000008569 process Effects 0.000 abstract description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 4
- 229910052760 oxygen Inorganic materials 0.000 abstract description 4
- 239000001301 oxygen Substances 0.000 abstract description 4
- 238000012546 transfer Methods 0.000 abstract description 4
- 239000000126 substance Substances 0.000 abstract description 3
- 239000012530 fluid Substances 0.000 abstract description 2
- 238000011065 in-situ storage Methods 0.000 abstract 1
- 238000006276 transfer reaction Methods 0.000 abstract 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 20
- 229910052757 nitrogen Inorganic materials 0.000 description 10
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 8
- 229920002472 Starch Polymers 0.000 description 6
- 239000008107 starch Substances 0.000 description 6
- 235000019698 starch Nutrition 0.000 description 6
- 239000012535 impurity Substances 0.000 description 4
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 4
- 238000011160 research Methods 0.000 description 4
- CKUAXEQHGKSLHN-UHFFFAOYSA-N [C].[N] Chemical compound [C].[N] CKUAXEQHGKSLHN-UHFFFAOYSA-N 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000010170 biological method Methods 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000003995 emulsifying agent Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 239000002352 surface water Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 206010059866 Drug resistance Diseases 0.000 description 1
- 241000282414 Homo sapiens Species 0.000 description 1
- NWGKJDSIEKMTRX-AAZCQSIUSA-N Sorbitan monooleate Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OC[C@@H](O)[C@H]1OC[C@H](O)[C@H]1O NWGKJDSIEKMTRX-AAZCQSIUSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 238000006136 alcoholysis reaction Methods 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 230000002146 bilateral effect Effects 0.000 description 1
- 238000006065 biodegradation reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 230000004720 fertilization Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/10—Packings; Fillings; Grids
- C02F3/105—Characterized by the chemical composition
- C02F3/108—Immobilising gels, polymers or the like
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
-
- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J7/00—Circuit arrangements for charging or depolarising batteries or for supplying loads from batteries
- H02J7/14—Circuit arrangements for charging or depolarising batteries or for supplying loads from batteries for charging batteries from dynamo-electric generators driven at varying speed, e.g. on vehicle
- H02J7/1423—Circuit arrangements for charging or depolarising batteries or for supplying loads from batteries for charging batteries from dynamo-electric generators driven at varying speed, e.g. on vehicle with multiple batteries
-
- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02J—CIRCUIT ARRANGEMENTS OR SYSTEMS FOR SUPPLYING OR DISTRIBUTING ELECTRIC POWER; SYSTEMS FOR STORING ELECTRIC ENERGY
- H02J7/00—Circuit arrangements for charging or depolarising batteries or for supplying loads from batteries
- H02J7/34—Parallel operation in networks using both storage and other dc sources, e.g. providing buffering
- H02J7/35—Parallel operation in networks using both storage and other dc sources, e.g. providing buffering with light sensitive cells
-
- H—ELECTRICITY
- H02—GENERATION; CONVERSION OR DISTRIBUTION OF ELECTRIC POWER
- H02S—GENERATION OF ELECTRIC POWER BY CONVERSION OF INFRARED RADIATION, VISIBLE LIGHT OR ULTRAVIOLET LIGHT, e.g. USING PHOTOVOLTAIC [PV] MODULES
- H02S10/00—PV power plants; Combinations of PV energy systems with other systems for the generation of electric power
- H02S10/10—PV power plants; Combinations of PV energy systems with other systems for the generation of electric power including a supplementary source of electric power, e.g. hybrid diesel-PV energy systems
- H02S10/12—Hybrid wind-PV energy systems
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/009—Apparatus with independent power supply, e.g. solar cells, windpower or fuel cells
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2203/00—Apparatus and plants for the biological treatment of water, waste water or sewage
- C02F2203/006—Apparatus and plants for the biological treatment of water, waste water or sewage details of construction, e.g. specially adapted seals, modules, connections
-
- 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
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Microbiology (AREA)
- Chemical & Material Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Biodiversity & Conservation Biology (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Power Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
The invention discloses a hydraulic spinning biological film purifying system for a small micro water body and a working method thereof, and the hydraulic spinning biological film purifying system comprises a box body, wherein the upper surface of the box body is fixedly connected with a wind plate module and a solar plate module, the front end and the rear end of the box body are fixedly connected with a grid module, the upper surface of the interior of the box body is fixedly connected with an integrated electric control module, the left end of the box body is provided with a water wheel, the right end of the water wheel is fixedly connected with a transmission shaft, the interior of the box body is provided with a rotating mechanism, the upper part of the rotating mechanism is provided with a rocker mechanism, the left side of the rocker mechanism is provided with a reciprocating motion mechanism, a hydraulic spinning device is arranged, a biological film filler is embedded in the hydraulic spinning device, the multiphase fluid mass transfer process in a filler system can be improved, the utilization efficiency of a biological film to oxygen is improved, the mass transfer reaction process of a substance is promoted, the biological film filler can increase the carbon content of the water body through carbon release, and the in-situ biological denitrification effect is improved.
Description
Technical Field
The invention belongs to the technical field of water purification, and particularly relates to a hydraulic spin biological membrane purification system for a small micro water body and a working method thereof.
Background
Due to excessive fertilization and industrial production activities, a large amount of nitrogen-containing compounds enter small micro-water bodies such as rivers and lakes with poor self-cleaning capability, however, when the ammonia nitrogen content in the small micro-water bodies is too high, a series of serious environmental problems such as water eutrophication, reduction of aquatic organism diversity and the like are caused, and finally, the influence on the life health and safety of human beings is generated. At present, ammonia nitrogen becomes a parameter index which is primarily examined in water pollution in China. According to the research in recent years, the occurrence frequency of ammonia nitrogen in surface water body out-of-standard pollutants in China is very high, and the trend of increasing year by year is shown, for example, the ammonia nitrogen content of other water systems except for Zhujiang and Changjiang in seven water systems exceeds the ammonia nitrogen limit value (0.5 mg/L) in sanitary Standard for Drinking Water (GB 5749-2006), and in addition, the ammonia nitrogen content in water systems in a plurality of places in China is above 4mg/L, and even reaches 50.4mg/L at most. Therefore, the problem of ammonia nitrogen pollution in surface water is solved, and the method becomes important content in the field of water treatment in China.
The pollution control technology currently available for small micro water bodies with too high nitrogen content mainly comprises a physical method, a chemical method and a biological method. From the viewpoints of thoroughly eliminating nitrogen pollution and reducing economic cost, the heterotrophic nitrification and aerobic denitrification process by a biological method is most reasonable in the technologies. The process can use organic carbon as an electron donor, resulting in a higher nitrification-denitrification rate. However, the lack of available carbon sources is a worldwide problem in the heterotrophic nitrification aerobic denitrification of small micro-bodies of water with low carbon to nitrogen ratios. At present, the research on the carbon source adopted by the heterotrophic nitrification-aerobic denitrification process is mainly focused on the deep development and utilization of the system carbon source and the accurate addition control aspect of the traditional additional carbon source, and the research and engineering application of the emerging slow-release carbon source to promote the characteristics of nitrification-denitrification are less. In addition, the water body is generally purified by adding a slow-release carbon source, and the polluted water body such as rivers and lakes is easy to run off, the contact area time is short, and the purifying effect is poor. The slow-release carbon source is used as a material and is used as a carrier for the growth of a biological film to promote the biological removal of pollutants, and the slow-release carbon source can also be used for providing a carbon source for a water body with a low carbon nitrogen ratio, so that the removal rate of nitrogen in the water body is improved. Based on the background, the invention provides the biological film filler hydraulic spinning device with the carbon source slow-release function, so that the water quality of the small micro water body is purified and improved.
Disclosure of Invention
The invention aims to provide a hydraulic spinning biological membrane purifying system for a small micro water body and a working method thereof, and solves the problems in the background technology by arranging a hydraulic spinning device with biological membrane filler.
In order to achieve the above purpose, the present invention provides the following technical solutions: the utility model provides a water conservancy spins biomembrane clean system for little water, includes the box, the fixedly connected with wind-force board module and solar panel module on the box, both ends fixedly connected with grid module around the box, the inside upper surface fixedly connected with integrated electronic control module of box, integrated electronic control module bilateral symmetry fixedly connected with electric telescopic handle, the box left end is provided with the water wheel, water wheel right-hand member fixedly connected with transmission shaft, wind-force board module utilizes wind-driven wind-force board, turns into the electric energy with wind energy, realizes wind power generation's purpose, provides electric energy support for subsequent system, solar panel module absorbs solar energy, turns into the electric energy with solar energy, realizes solar energy power generation's purpose, provides electric energy support for subsequent system, grid module is used for the separation to possibly get into the system withered branch rotten leaf and the large-block rubble, the inside rotary mechanism that is provided with of box, rotary mechanism includes the water conservancy and spins the device, the inside biomembrane filler that is provided with of water wheel, the rotary mechanism top is provided with rocker mechanism, rocker mechanism left side is provided with reciprocating motion.
Preferably, the center of the hydraulic spinning device is fixedly connected with a connecting shaft in a penetrating mode, the top end of the connecting shaft is fixedly connected with a rotating gear, and the rotating gear is connected with a rack in a meshed mode.
Preferably, the hydraulic spinning device is internally embedded with a biological film filler, the biological film filler has a cylindrical strip structure with the diameter of about 5mm, the length is consistent with the height of the hydraulic spinning device, the bulk specific gravity of the biological film filler is in the range of 70-100kg/m, the nitrification efficiency of the hydraulic spinning device is in the range of 800-1600 g/m.d, and the BOD oxidation efficiency and the COD oxidation efficiency of the biological film filler are both in the range of 1500-8000 g/m.d.
Preferably, the reciprocating mechanism comprises two supporting tables, a guide rod and a driven shaft are fixedly connected between the two supporting tables, a cylindrical cam is fixedly sleeved on the outer ring of the driven shaft, a sliding groove is formed in the surface of the cylindrical cam, a rotating column is slidably connected to the bottom end of the sliding groove, a sliding block is rotatably connected to the bottom end of the rotating column, and the sliding block slides on the guide rod.
Preferably, the supporting table extends to the bottom of the box body and is fixedly connected with the supporting table, four reciprocating mechanisms are arranged in total and are fixedly connected in pairs, the left end of the driven shaft positioned at the upper left part is fixedly connected with the transmission shaft, and the right end of the driven shaft positioned at the lower left part is rotatably connected with the inner wall of the box body.
Preferably, the rocker mechanism comprises a driving crank wheel, a fixed shaft is fixedly connected to the middle part of the left end of the driving crank wheel, a first crank shaft is fixedly connected to the left end of the driving crank wheel at a position deviating from the circle center, a connecting rod is rotatably connected to the outer ring of the first crank shaft, a second crank shaft is rotatably connected to the other end of the connecting rod, a driven crank wheel is fixedly connected to the other end of the second crank shaft, and a rotating shaft is fixedly connected to the left end of the driven crank wheel.
Preferably, the right ends of the driving crank wheel and the driven crank wheel are fixedly connected with the corresponding driven shafts, and the upper surface of the connecting rod is always parallel to the upper surface of the box body.
The invention also provides a working method of the hydraulic spin biological membrane purification system for the small micro water body, which comprises the following steps:
s1: the grid module firstly filters out dead branches, rotten leaves and large broken stones, weakens water flow impact and protects the hydraulic spinning device;
s2: the wind power plate module and the solar power plate module respectively absorb wind energy and solar energy and convert the wind energy and the solar energy into electric energy for storage;
s3: the integrated electronic control module detects whether the speed of the water wheel reaches a preset critical speed;
s4: if the electric energy is not reached, the integrated electric control module releases the stored electric energy to drive the transmission shaft to rotate, and if the electric energy is reached, the transmission shaft is driven to rotate by the water wheel;
s5: the water flow passes through the hydraulic spinning device which reciprocates and rotates by itself to carry out biological membrane purification.
Compared with the prior art, the invention has the beneficial effects that:
1. according to the invention, the hydraulic spinning device is arranged, the biofilm filler is embedded in the hydraulic spinning device, and the biofilm filler is a novel polymer slow-release carbon source material prepared from polyvinyl alcohol and sodium acetate serving as raw materials, so that the novel polymer slow-release carbon source material can be used as a filler to provide a carrier for microbial growth, can increase the release amount of a carbon source, can improve the carbon nitrogen ratio, can promote small micro water bodies to achieve a better purifying effect, and can not cause secondary pollution to the water bodies.
2. According to the invention, through arranging the integrated electric control module, the solar panel module and the wind panel module, two driving modes of the hydraulic spinning device are realized, electric energy is saved when water flow is fast, spinning is performed by means of the water flow, the purifying effect is improved, and the stored electric energy driving device can be released to spin and purify when the water flow is slow.
3. The reciprocating mechanism, the rocker mechanism and the rotating mechanism are arranged, so that the hydraulic spinning device is enabled to reciprocate in a staggered way by taking water flow as power and rotate by itself, the multiphase fluid mass transfer process in the filling system is improved, the utilization efficiency of the biomembrane to oxygen is promoted, and the water quality purifying effect is improved.
Drawings
FIG. 1 is a schematic diagram of the overall structure of the present invention;
FIG. 2 is a side cross-sectional view of the internal structure of the present invention
FIG. 3 is a bottom cross-sectional view of the internal structure of the present invention;
FIG. 4 is a schematic illustration of the internal structure of the present invention;
FIG. 5 is a schematic view of the structure of the water wheel of the present invention;
FIG. 6 is a front elevational view of the reciprocating mechanism of the present invention;
FIG. 7 is a schematic view of a rocker mechanism according to the present invention;
FIG. 8 is a schematic view of a rotary mechanism according to the present invention;
FIG. 9 is a schematic view of the structure of the slider in the reciprocating mechanism of the present invention;
FIG. 10 is a schematic diagram of a hydraulic spinning device according to the present invention;
FIG. 11 is a flow chart of a method of operation of the present invention;
FIG. 12 is a graph showing the nitrogen removal rate of a biofilm carrier (JC) prepared from polyvinyl alcohol and sodium acetate according to the invention compared with that of a biofilm carrier of conventional material (polyvinyl alcohol and starch);
in the figure: 1. a case; 2. a wind panel module; 3. a solar panel module; 4. a grid module; 5. integrating an electric control module; 6. a water wheel; 7. a transmission shaft; 8. an electric telescopic rod; 100. a reciprocating mechanism; 101. a support table; 102. a guide rod; 103. a driven shaft; 104. a slide block; 105. a rotating column; 106. a cylindrical cam; 107. a chute; 200. a rocker mechanism; 201. a driving crank wheel; 202. a fixed shaft; 203. a first crank shaft; 204. a connecting rod; 205. a second crank shaft; 206. a rotating shaft; 207. a driven crank wheel; 300. a rotation mechanism; 301. rotating the gear; 302. a connecting shaft; 303. a rack; 304. a hydraulic spinning device; 305. biofilm packing.
Detailed Description
The following description of the embodiments of the present invention will be made clearly and fully with reference to the accompanying drawings, in which it is evident that the embodiments described are only some, but not all embodiments of the invention. The components of the embodiments of the present invention generally described and illustrated in the figures herein may be arranged and designed in a wide variety of different configurations. Thus, the following detailed description of the embodiments of the invention, as presented in the figures, is not intended to limit the scope of the invention, as claimed, but is merely representative of selected embodiments of the invention. All other embodiments, which can be made by a person skilled in the art without making any inventive effort, are intended to be within the scope of the present invention.
The research and engineering application reports of the denitrification promotion characteristic of the new slow-release carbon source for river and lake water purification treatment are less.
Referring to fig. 1 to 12, the present invention provides a technical solution: the utility model provides a water conservancy spins biomembrane clean system for little water, including box 1, the fixed surface is connected with wind-force board module 2 and solar panel module 3 on the box 1, both ends fixedly connected with grid module 4 around the box 1, the inside upper surface fixedly connected with integrated electronic control module 5 of box 1, integrated electronic control module 5 both sides symmetry fixedly connected with electric telescopic handle 8, the box 1 left end is provided with water wheels 6, water wheels 6 right-hand member fixedly connected with transmission shaft 7, wind-force board module 2 utilizes wind-driven wind-force board, convert wind energy into electric energy, realize wind-powered generation's purpose, provide electric energy support for follow-up system, solar panel module 3 absorbs solar energy, convert solar energy into electric energy, realize solar energy power generation's purpose, provide electric energy support for follow-up system, grid module 4 is used for the separation to get into the rotten leaf of dead branch in the system and big rubble, the inside rotary mechanism 300 that is provided with of box 1, rotary mechanism 300 includes the water conservancy and spinning device 304, water conservancy spinning device 304 is formed by the biomembrane filler, rotary mechanism 300 top is provided with rocker mechanism 200, rocker mechanism 200 left side is provided with reciprocating motion mechanism 100.
In order to improve the water quality purifying effect, the center of the hydraulic spinning device 304 is fixedly connected with a connecting shaft 302 in a penetrating manner, the top end of the connecting shaft 302 is fixedly connected with a rotary gear 301, the rotary gear 301 is connected with a rack 303 in a meshed manner, the specification of the biological film filler 305 is of a cylindrical strip structure with the diameter of about 5mm, the length of the biological film filler is consistent with the height of the hydraulic spinning device, the bulk specific gravity of the biological film filler 305 is in the range of 70-100kg/m, the nitrification efficiency of the biological film filler 305 is between 800-1600 g/m.d, the BOD oxidation efficiency and the COD oxidation efficiency of the biological film filler 305 are both between 1500-8000 g/m.d, and in order to improve the purifying efficiency of the rotary mechanism 300 on water bodies, a plurality of rotary mechanisms 300 can be arranged in the box body 1, and the rotary mechanisms 300 work simultaneously to increase the contact area and the contact time of the biological film filler 305 and the water bodies so as to improve the purifying efficiency of the rotary mechanism 300 on the water bodies.
Specifically, the preparation method of the biofilm pack 305 in the invention comprises the following steps: adding polyvinyl alcohol into water, stirring, and heating to 98 ℃ to form a stable solution; in the step, 10-50 parts by weight of polyvinyl alcohol and 90-100 parts by weight of water are used; wherein the average polymerization degree of the polyvinyl alcohol is 1700 and the alcoholysis degree is 99 percent; step b: adding sodium acetate into water, stirring, and forming a solution; in the step, 10-50 parts by weight of sodium acetate and 100 parts by weight of water are taken; step c, adding sodium acetate solution into the stable solution, and stirring and mixing uniformly; step d: pouring into a mould, solidifying in a freezer, cutting into blocks, and immersing in emulsifying agent; the emulsifier adopted in the specific step is SPAN80, the temperature of the freezer is-70 ℃, and the curing time is 4-12 hours.
The filler with the slow-release carbon source prepared by the preparation method can reduce the additional carbon source in the ammonia nitrogen wastewater treatment process, has good hydrophilic performance and high porosity, is beneficial to the adhesion and survival of microorganisms, and ensures the sewage treatment effect.
In order to realize the reciprocating motion of the hydraulic spinning device, the reciprocating motion mechanism 100 comprises two supporting tables 101, a guide rod 102 and a driven shaft 103 are fixedly connected between the two supporting tables 101, a cylindrical cam 106 is fixedly sleeved on the outer ring of the driven shaft 103, a sliding groove 107 is formed in the surface of the cylindrical cam 106, a rotating column 105 is slidably connected to the bottom end of the sliding groove 107, a sliding block 104 is rotatably connected to the bottom end of the rotating column 105, and the sliding block 104 slides on the guide rod 102. The supporting table 101 extends to the bottom of the box body 1 and is fixedly connected with the box body 1, four reciprocating mechanisms 100 are arranged in total and are fixedly connected in pairs, the left end of a driven shaft 103 positioned at the upper left is fixedly connected with the transmission shaft 7, and the right end of the driven shaft 103 positioned at the lower left is rotatably connected with the inner wall of the box body 1.
In order to realize the staggered movement of the front and rear hydraulic spinning devices, the rocker mechanism 200 comprises a driving crank wheel 201, a fixed shaft 202 is fixedly connected to the middle of the left end of the driving crank wheel 201, a first crank shaft 203 is fixedly connected to the left end of the driving crank wheel 201 at a position deviating from the circle center, a connecting rod 204 is rotatably connected to the outer ring of the first crank shaft 203, the other end of the connecting rod 204 is rotatably connected with a second crank shaft 205, a driven crank wheel 207 is fixedly connected to the other end of the second crank shaft 205, and a rotating shaft 206 is fixedly connected to the left end of the driven crank wheel 207. The right ends of the driving crank wheel 201 and the driven crank wheel 207 are fixedly connected with the corresponding driven shafts 103, and the upper surface of the connecting rod 204 is always parallel to the upper surface of the box body 1.
The working method of the hydraulic spin biological film purifying system for the small micro water body is characterized by comprising the following steps of:
s1: the grid module 4 firstly filters out dead branches, rotten leaves and large broken stones and weakens the impact of water flow on the biofilm packing 305, and protects the hydraulic spinning device 304; when more impurities are accumulated on the surface of the grid module 4, the electric telescopic rod 8 starts to work to drive the grid module 4 to move so as to shake off the impurities on the surface of the grid module 4, so that the impurities are prevented from accumulating on the surface of the grid module 4 and prevent water from flowing into the purification system;
s2: the wind plate module 2 and the solar plate module 3 respectively absorb wind energy and solar energy and convert the wind energy and the solar energy into electric energy for storage;
s3: the integrated electronic control module 5 detects whether the speed of the water wheel 6 reaches a preset critical speed;
s4: if the electric energy is not reached, the integrated electric control module 5 releases the stored electric energy to drive the transmission shaft 7 to rotate, and if the electric energy is reached, the transmission shaft 7 is automatically driven to rotate through the water wheel 6;
s5: the water flow passes through the hydraulic spinning device 304 which reciprocates and rotates itself for biological membrane purification.
The working principle of the invention is as follows: filtering large-particle impurities such as dead branches, rotten leaves, large broken stones and the like from the sewage through a steel grid; after that, when the flow speed of the water flow is large enough, the water flow is continuously rotated by the hydraulic spinning device 304, so that a strong turbulence effect is formed, the biological film is fully contacted with pollutants in the water, the transfer of organic matters between a liquid phase and a biological phase is effectively enhanced, in addition, the rotation of the hydraulic spinning device 304 has a cutting effect on oxygen, the mass transfer effect of the oxygen is further enhanced, and the purpose of high-efficiency water purification is realized; when the flow rate of the water flow is low, the integrated electronic control module 5 immediately intervenes to release the electric energy collected by the wind plate module 2 and the solar plate module 3 in the earlier stage so that the hydraulic spinning device 304 keeps a stable rotating speed.
The biomembrane filler used by the hydraulic spinning device is a microporous polymer material (JC for short) with high porosity and high specific surface area which is independently developed, is prepared from polyvinyl alcohol and sodium acetate serving as raw materials and has a carbon source slow release function, can provide a carrier for microorganism growth, can increase the release amount of the carbon source, improves the carbon nitrogen ratio, promotes small micro water bodies to achieve better purification effect, and does not cause secondary pollution to the water bodies; wherein JC organismThe relevant parameters for the application of the membrane filler in the system are shown below: specific surface area greater than 900m 2 And/m < W >, the film forming time is 7-15d, the application temperature is 2-70 ℃, and the service life is 8-10 a. Application characteristics of JC biofilm packing in a system: light weight, floatability, light weight, impact resistance and floatability, energy conservation and freight and running cost saving; environmental protection, no pollution and no chemical residue; the film forming performance is good, the porosity is high, the specific surface area is large, and the bacterial growth is facilitated; the film forming speed is high, the biocompatibility is good, and the film forming time is shortened to 7-15 days; oil resistance, drug resistance, stable material, acid resistance, alkali resistance, aging resistance and biodegradation resistance.
The nitrogen removal rate of the biofilm carrier (JC) prepared from polyvinyl alcohol and sodium acetate is compared with that of the biofilm carrier made from conventional materials (polyvinyl alcohol and starch) as shown in FIG. 12. Adding 5g of slow-release carbon source biomembrane filler (the proportion of the used filler raw materials is that of polyvinyl alcohol: starch=1:1)) into a reactor, then adding 100mL of domesticated activated sludge and 400mL of test water (50 mg/L of simulated nitrogenous wastewater), sealing a bottle mouth by using a sealing film, and keeping the anoxic environment in the reactor. And placed in a shaking box at a set speed of 70rpm for culture reaction. And measuring and calculating the removal rate of nitrogen in the nitrogen-containing wastewater after 24 hours, and replacing the nitrogen-containing wastewater in the reactor every 24 hours without replacing slow-release carbon source biofilm filler in the reactor. The experiment was continued for 20 days. Comparison experiments are carried out by adopting sodium acetate to replace starch under the same test conditions, and the comparison of the nitrogen removal rate of the novel biological film filler (JC) prepared by polyvinyl alcohol and sodium acetate and the conventional biological film filler prepared by polyvinyl alcohol and starch in the range of 20 days shows that the nitrogen removal rate of the novel biological film filler of JC is always above 85 percent and can reach 95 percent; the nitrogen removal rate of the conventional biological film filler prepared from the polyvinyl alcohol and the starch which are commonly used at present is far better than that of the conventional biological film filler, so that the biological film filler can play an important forward pushing role in purifying the water quality of small and micro water bodies when being used in the system.
The invention drives the driven shaft 103 to rotate through the transmission shaft 7, so that the sliding block 104 slides on the sliding groove 107 on the cylindrical cam 106, and then drives the sliding block 104 to slide on the guide rod 102, so that the guide rod 102 drives the rotary gear 301 to move left and right, the rotary gear 301 drives the hydraulic spinning device 304 to rotate through the connecting shaft 302 under the action of the rack 303, and thus the reciprocating motion and spinning motion of the hydraulic spinning device 304 are realized, four reciprocating motion mechanisms 100, a rocker mechanism 200 and a rotating mechanism 300 are provided, the transmission shaft 7 drives the driven shaft 103 to rotate, and simultaneously, the driven shaft 103 drives the driving crank wheel 201 to rotate, so that the fixed shaft 202 drives the connecting rod 204 to do circular motion, and then the second crank shaft 205 drives the driven crank wheel 207 to do circular motion, so that the hydraulic spinning device 304 on the left side reciprocates and spins, and the hydraulic spinning devices 304 on the left side and the right side are always staggered in the process, and the water purifying effect on the water body is improved.
While embodiments of the present invention have been shown and described, it will be understood by those of ordinary skill in the art that: many changes, modifications, substitutions and variations may be made to the embodiments without departing from the spirit and principles of the invention, the scope of which is defined by the claims and their equivalents.
Claims (4)
1. The utility model provides a water conservancy spins biomembrane clean system for little water, includes box (1), fixed surface is connected with wind-force board module (2) and solar panel module (3) on box (1), both ends fixedly connected with grid module (4) around box (1), fixed surface is connected with integrated automatically controlled module (5) on box (1), integrated automatically controlled module (5) both sides fixedly connected with electric telescopic handle (8), box (1) left end is provided with water wheels (6), water wheels (6) right-hand member fixedly connected with transmission shaft (7), wind-force board module (2) utilize wind-driven wind-force board, with wind energy conversion for the purpose of wind power generation, for the purpose of providing electric energy support of follow-up system, solar panel module (3) absorb solar energy, with solar energy conversion for the electric energy, realize solar energy power generation's purpose, provide electric energy support for follow-up system, grid module (4) are used for obstructing the rotten leaf of wither in probably getting into the system and big piece, its characterized in that: the biological membrane filter comprises a box body (1), and is characterized in that a rotating mechanism (300) is arranged inside the box body (1), the rotating mechanism (300) comprises a hydraulic spinning device (304), a biological membrane filler (305) is arranged inside the hydraulic spinning device (304), a rocker mechanism (200) is arranged above the rotating mechanism (300), and a reciprocating mechanism (100) is arranged on the left side of the rocker mechanism (200);
the hydraulic spinning device (304) is embedded with a biomembrane filler (305), when the flow rate of water flow is large enough, the hydraulic spinning device (304) continuously rotates under the action of the water flow, and when the flow rate of water flow is low, the integrated electronic control module (5) immediately intervenes to release electric energy collected by the wind plate module (2) and the solar plate module (3) in the early stage so that the hydraulic spinning device (304) keeps a stable rotating speed;
the reciprocating mechanism (100) comprises two supporting tables (101), a guide rod (102) and a driven shaft (103) are fixedly connected between the two supporting tables (101), a cylindrical cam (106) is fixedly sleeved on the outer ring of the driven shaft (103), a sliding groove (107) is formed in the surface of the cylindrical cam (106), a rotating column (105) is slidably connected to the bottom end of the sliding groove (107), a sliding block (104) is rotatably connected to the bottom end of the rotating column (105), and the sliding block (104) slides on the guide rod (102);
the supporting table (101) extends to the bottom of the box body (1) and is fixedly connected with the box body, four reciprocating mechanisms (100) are arranged in total and are fixedly connected with each other, the left end of the driven shaft (103) positioned at the upper left part is fixedly connected with the transmission shaft (7), and the right end of the driven shaft (103) positioned at the lower left part is rotatably connected with the inner wall of the box body (1);
the rocker mechanism (200) comprises a driving crank wheel (201), a fixed shaft (202) is fixedly connected to the middle of the left end of the driving crank wheel (201), a first crank shaft (203) is fixedly connected to the left end of the driving crank wheel (201) at the position deviating from the circle center, a connecting rod (204) is rotatably connected to the outer ring of the first crank shaft (203), a second crank shaft (205) is rotatably connected to the other end of the connecting rod (204), a driven crank wheel (207) is fixedly connected to the other end of the second crank shaft (205), and a rotating shaft (206) is fixedly connected to the left end of the driven crank wheel (207);
the right ends of the driving crank wheel (201) and the driven crank wheel (207) are fixedly connected with the corresponding driven shafts (103), and the upper surface of the connecting rod (204) is always parallel to the upper surface of the box body (1);
the biofilm pack (305) is prepared from polyvinyl alcohol and sodium acetate, and the proportion of the polyvinyl alcohol and the sodium acetate in the biofilm pack (305) is 1:1.
2. a hydraulic spin biofilm purification system for small micro bodies of water according to claim 1 wherein: the center of the hydraulic spinning device (304) is fixedly connected with a connecting shaft (302) in a penetrating mode, the top end of the connecting shaft (302) is fixedly connected with a rotating gear (301), and the rotating gear (301) is connected with a rack (303) in a meshed mode.
3. A hydraulic spin biofilm purification system for small micro bodies of water according to claim 2 wherein: the biofilm packing (305) has a bulk specific gravity of 70-100kg/m 3 Within the range, the nitrification efficiency of the hydraulic spinning device (304) is 800-1600g/m 3 D, the BOD oxidation efficiency and the COD oxidation efficiency of the biological film filling material (305) are both in the range of 1500-8000g/m 3 ·d。
4. A method of operating a hydraulic spin biofilm purification system for small micro bodies of water as claimed in claim 3 and characterised in that:
s1: the grid module (4) firstly filters out dead branches, rotten leaves and large broken stones and weakens the impact of water flow, and protects the hydraulic spinning device (304);
s2: the wind power board module (2) and the solar power board module (3) respectively absorb wind energy and solar energy and convert the wind energy and the solar energy into electric energy for storage;
s3: the integrated electronic control module (5) detects whether the speed of the water wheel (6) reaches a preset critical speed or not;
s4: if the electric energy is not reached, the integrated electric control module (5) releases the stored electric energy to drive the transmission shaft (7) to rotate, and if the electric energy is reached, the transmission shaft (7) is automatically driven to rotate through the water wheel (6);
s5: the water flow passes through a hydraulic spinning device (304) which reciprocates and rotates by itself to carry out biological film purification.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210937440.4A CN115215427B (en) | 2022-08-05 | 2022-08-05 | Hydraulic spin biological membrane purification system for small micro water body and working method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202210937440.4A CN115215427B (en) | 2022-08-05 | 2022-08-05 | Hydraulic spin biological membrane purification system for small micro water body and working method |
Publications (2)
Publication Number | Publication Date |
---|---|
CN115215427A CN115215427A (en) | 2022-10-21 |
CN115215427B true CN115215427B (en) | 2023-04-25 |
Family
ID=83615803
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202210937440.4A Active CN115215427B (en) | 2022-08-05 | 2022-08-05 | Hydraulic spin biological membrane purification system for small micro water body and working method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN115215427B (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112028230A (en) * | 2020-08-27 | 2020-12-04 | 盐城工学院 | Combined biological filler with self-spinning function |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7736508B2 (en) * | 2006-09-18 | 2010-06-15 | Christopher A. Limcaco | System and method for biological wastewater treatment and for using the byproduct thereof |
RU80843U1 (en) * | 2008-08-29 | 2009-02-27 | Николай Иванович Куликов | BLOCK MODULE OF BIOLOGICAL CLEANING OF CITY WASTE WATERS IN THE CONDITIONS OF SIBERIA |
CN102815785A (en) * | 2012-08-30 | 2012-12-12 | 北京工业大学 | Preparation method of encapsulated solid-phase slow-release composite carbon source |
CN111285460B (en) * | 2020-01-23 | 2022-06-14 | 浙江开创环保科技股份有限公司 | Energy-saving, consumption-reducing and pollution-resistant MBR system |
CN111635000A (en) * | 2020-06-13 | 2020-09-08 | 河南泽衡环保科技股份有限公司 | Production device of high-efficiency biological membrane |
CN214088163U (en) * | 2020-12-13 | 2021-08-31 | 江西省新建润泉供水有限公司 | Ecological restoration mechanism for water purification |
CN113698040B (en) * | 2021-09-03 | 2022-11-18 | 中国科学院地理科学与资源研究所 | Multifunctional ecological restoration device for non-point source pollution of Yangtze river basin |
-
2022
- 2022-08-05 CN CN202210937440.4A patent/CN115215427B/en active Active
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112028230A (en) * | 2020-08-27 | 2020-12-04 | 盐城工学院 | Combined biological filler with self-spinning function |
Also Published As
Publication number | Publication date |
---|---|
CN115215427A (en) | 2022-10-21 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103359834B (en) | Wind and light coupled oxygen-enriched nanometer matrix composite ecological floating bed | |
CN111285462B (en) | Synergistic denitrification composite suspended filler, preparation method and application thereof | |
CN105481206B (en) | A kind of control method of black smelly river lake original position ecological reestablishment integrated system | |
CN1341079A (en) | Magnetic sludge suitable for use in waste water treatment and method for preparing same and method for waste water treatment | |
CN103708619A (en) | Fluidized bed biofilm filler, and preparation method and filler structure thereof | |
CN101691547A (en) | Method for restoring micro-scale polluted reservoir water by using situ bio-contact oxidation | |
CN211712741U (en) | Micro-power ecological floating bed combined water purification system | |
CN103232138A (en) | Combined constructed wetland treatment method and system for nitrobenzene wastewater | |
CN101338292A (en) | Method for preparing immobilization cold resistant strain | |
CN109179635A (en) | A kind of microorganism ball, preparation method and the application of black and odorous water river bottom mud of degrading | |
CN205398375U (en) | Black smelly river lake normal position ecological remediation technique integrated system | |
CN103951079A (en) | Preparation and application of denitrifying bacteria immobilized bioactive filler based on polyurethane carrier | |
CN115215427B (en) | Hydraulic spin biological membrane purification system for small micro water body and working method | |
CN202688153U (en) | Deep treatment device of municipal sewage | |
CN108408909B (en) | Ecological adsorption floating bed main body for water eutrophication treatment | |
CN203820528U (en) | Cellular structural biological rotating disc | |
CN107986557B (en) | Coupling biological treatment process for synchronously removing nitrogen and phosphorus in agricultural runoff | |
CN206843179U (en) | One kind spin floatation type combined stuffing bioreactor | |
CN115520961A (en) | Diatomite reinforcement-based high ammonia nitrogen wastewater nitrosation treatment method | |
CN114455784A (en) | Online direct drainage treatment method and treatment equipment for fecal sewage in vehicle-mounted toilet of high-speed rail motor train unit | |
CN2515197Y (en) | Floating-bed type sewage purifier with wind energy aeration and biological treatment | |
CN103253769B (en) | The biological membrane-transferring device of automatic oxygenation formula | |
CN105084553A (en) | Biochar based spiral magnetic bio-membrane reactor | |
CN109368934B (en) | Autotrophic denitrification device for wastewater and wastewater treatment method | |
CN208308529U (en) | Mobile bionic aquatic weed |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |