CN202079073U - Real-time treatment system using high-energy oxygen for hydrolyzing and oxidizing organic biomass - Google Patents
Real-time treatment system using high-energy oxygen for hydrolyzing and oxidizing organic biomass Download PDFInfo
- Publication number
- CN202079073U CN202079073U CN2011201488279U CN201120148827U CN202079073U CN 202079073 U CN202079073 U CN 202079073U CN 2011201488279 U CN2011201488279 U CN 2011201488279U CN 201120148827 U CN201120148827 U CN 201120148827U CN 202079073 U CN202079073 U CN 202079073U
- Authority
- CN
- China
- Prior art keywords
- tank
- micro
- slurry
- nano bubble
- organic
- 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.)
- Expired - Fee Related
Links
- 239000001301 oxygen Substances 0.000 title claims abstract description 32
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 32
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 29
- 239000002028 Biomass Substances 0.000 title abstract 6
- 230000003301 hydrolyzing effect Effects 0.000 title abstract 2
- 230000001590 oxidative effect Effects 0.000 title abstract 2
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 50
- 230000003647 oxidation Effects 0.000 claims abstract description 47
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 34
- 239000002101 nanobubble Substances 0.000 claims abstract description 34
- 239000002002 slurry Substances 0.000 claims abstract description 32
- 230000007062 hydrolysis Effects 0.000 claims abstract description 27
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 27
- 238000010525 oxidative degradation reaction Methods 0.000 claims abstract description 24
- 238000005273 aeration Methods 0.000 claims abstract description 22
- 229910001385 heavy metal Inorganic materials 0.000 claims abstract description 13
- 238000000034 method Methods 0.000 claims description 21
- 230000008569 process Effects 0.000 claims description 21
- 238000000746 purification Methods 0.000 claims description 14
- 239000012528 membrane Substances 0.000 claims description 11
- 238000009287 sand filtration Methods 0.000 claims description 9
- 239000002351 wastewater Substances 0.000 claims description 6
- 238000010298 pulverizing process Methods 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 30
- 239000010813 municipal solid waste Substances 0.000 abstract description 18
- 239000002699 waste material Substances 0.000 abstract description 4
- 238000004064 recycling Methods 0.000 abstract description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract description 2
- 239000001257 hydrogen Substances 0.000 abstract 1
- 229910052739 hydrogen Inorganic materials 0.000 abstract 1
- 239000008213 purified water Substances 0.000 abstract 1
- 239000004576 sand Substances 0.000 abstract 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 11
- 238000003672 processing method Methods 0.000 description 9
- 239000002361 compost Substances 0.000 description 7
- 239000007789 gas Substances 0.000 description 7
- 239000003344 environmental pollutant Substances 0.000 description 6
- 231100000719 pollutant Toxicity 0.000 description 6
- 239000007864 aqueous solution Substances 0.000 description 5
- 238000010411 cooking Methods 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 230000033001 locomotion Effects 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 239000010865 sewage Substances 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical group [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 238000011109 contamination Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 239000005416 organic matter Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 238000005520 cutting process Methods 0.000 description 3
- 238000000855 fermentation Methods 0.000 description 3
- 230000036541 health Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000005276 aerator Methods 0.000 description 2
- 244000052616 bacterial pathogen Species 0.000 description 2
- 239000003183 carcinogenic agent Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000009264 composting Methods 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 2
- 238000004880 explosion Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 150000002894 organic compounds Chemical class 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 241000255925 Diptera Species 0.000 description 1
- 241000726221 Gemma Species 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 241001148470 aerobic bacillus Species 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 231100000357 carcinogen Toxicity 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 238000002224 dissection Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- 239000004021 humic acid Substances 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 150000002475 indoles Chemical class 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000002906 microbiologic effect Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 235000012149 noodles Nutrition 0.000 description 1
- 150000002898 organic sulfur compounds Chemical class 0.000 description 1
- 230000024241 parasitism Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000003053 toxin Substances 0.000 description 1
- 231100000765 toxin Toxicity 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
- 239000003403 water pollutant Substances 0.000 description 1
Images
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Treatment Of Sludge (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The utility model relates to a real-time treatment system using high-energy oxygen for hydrolyzing and oxidizing organic biomass, which comprises an organic biomass crushing slurrying machine, a slurry ozone micro-nano bubble oxidative degradation tank and an aerobic oxidation treatment tank. The organic biomass crushing slurrying machine is connected with a slurry pH (potential of hydrogen) value adjusting tank; the slurry pH value adjusting tank is connected with the slurry ozone micro-nano bubble oxidative degradation tank; one side of the slurry ozone micro-nano bubble oxidative degradation tank is continuously connected with a depth hydrolysis and oxidation tank, a centrifugal dehydrator, a heavy metal filter film, a micro-nano bubble generator, an aeration tank and the aerobic oxidation treatment tank; the aerobic oxidation treatment tank is sequentially connected with a sand filter purifying tank and a purified water collecting tank; and the aeration tank is connected with the micro-nano bubble generator. The real-time treatment system has the advantages that harmless treatment for the organic biomass of domestic garbage and kitchen garbage is completed rapidly, waste is turned into treasure, and a foundation is laid for recycling energy and resources in the organic biomass.
Description
Technical field
The utility model relates to a kind of with high energy oxygen hydrolysis oxidation organic-biological matter real time processing system.
Background technology
Organic-biological matter is the international difficult problem in the domestic rubbish disposal, also is most important pollution sources in the house refuse, still is the main component of rubbish from cooking simultaneously.It is the key that domestic rubbish disposal, catering trade rubbish from cooking are handled that organic-biological matter fast and harmless is handled, and has only the harm of thorough elimination organic-biological matter, could the calm processing of considering the Other Waste composition, satisfy that garbage disposal is innoxious, the requirement of minimizing.
The organic-biological matter processing mode mainstream technology of present domestic routine is landfill, burning, compost etc., and these processing means all can not be finished the fast and harmless of organic-biological matter and rubbish from cooking and handle, and therefore has great application limitation.For example, the landfill waste floor space is big, and according to incompletely statistics, the land area that China's garbage loading embeading takies has reached 50,000 square kilometres, is equivalent to 1/192 of China's territory gross area.Rubbish organic-biological matter generation anaerobic fermentation is very easily bred pathogenic bacteria, virus and other harmful organisms, especially garbage leachate soil and underground water source is caused severe contamination behind the landfill, and landfill gas is to causing serious air pollution around the refuse landfill.In addition, also there is the danger that sets off an explosion in the methane in the garbage loading embeading gas, and is unfavorable for social stability and community's harmony, and the resource of recyclable utilization is wasted fully in the rubbish.Though incineration treatment of garbage can be generated electricity or heat supply, there is the contradiction that investment is big, operation cost is high; China's house refuse calorific value is low, water content is big, and waste incineration also can produce strong carcinogen dioxin and nitrogen oxide, harm humans life security and health.The organic-biological matter compost treatment cycle long (one month), floor space is bigger, can constantly produce hydrogen sulfide, organic sulfur compound, indoles, aldehyde, the ketone material of the generation of kind more than totally 200 stench in the composting process, the severe contamination atmosphere, wherein kind belongs to carcinogenic substance more than 20.And can add stench and peculiar smell because of the corrupt substance that produces in the composting process, and cause mosquito, fly parasitism, become the epidemic disease carrier, influence environmental sanitation and publilc health.In addition, compost also produces methane, has hidden peril of explosion.In addition, compost fermentation sterilization degree is low, and hypopus of the harmful bacterium in the compost body (gemma) and heat-resisting pathogenic bacteria all grow in a large number, can accumulate a large amount of toxin and can produce secondary pollution to environment.At last, because active organic matter has been consumed by the long-term metabolism decomposition of microorganism, the organic matter that compost obtains is the nonactive organic matter of humic acids.Inorganic content height in the compost can destroy the physical arrangement in the soil.
Therefore above-mentioned various processing modes can not solve the substantive issue of garbage disposal, bigger secondary pollution are arranged, threatening environment safety and human health.
The processing of organic-biological matter is with minimizing and harmlessly turn to basic demand, and realize that minimizing and innoxious effective means are exactly to finish the oxidative degradation of organic-biological matter fast, organic-biological matter all is degraded to the small organic molecule of stablizing the carbon structure, eliminate the constitution water in the organic-biological matter, eliminate organic-biological matter fermentation function.
The utility model content
The purpose of this utility model provides a kind of with high energy oxygen hydrolysis oxidation organic-biological matter real time processing system, and the quick oxidative degradation of realization organic-biological matter reaches organic-biological matter and handles innoxious purpose.
The purpose of this utility model is to be achieved through the following technical solutions:
A kind of with high energy oxygen hydrolysis oxidation organic-biological matter real time processing system, comprise organic living beings pulverizing pulper, the micro-nano bubble oxidative degradation of the slurry ozone jar oxidation processes groove of becoming reconciled, described organic-biological matter is pulverized pulper and is connected with slurry pH value adjustment jar, the slurry pH value is adjusted jar and is connected with the micro-nano bubble oxidative degradation of slurry ozone jar, the micro-nano bubble oxidative degradation of slurry ozone jar is connected with depth hydrolysis's oxidation trough, depth hydrolysis's oxidation trough is connected with centrifugal dehydrator, centrifugal dehydrator is connected with the heavy metal filter membrane, the heavy metal filter membrane is connected with the aeration tank, described aeration tank is connected with the micro-nano bubble generator oxidation processes groove of becoming reconciled respectively again, good oxidation treatment trough is connected with the sand filtration purification tank, and the sand filtration purification tank connects the feeder of purifying waste water again.
The beneficial effects of the utility model are: finish the harmless treatment of house refuse organic-biological matter and rubbish from cooking fast, and turn waste into wealth, for the energy and the resource that reclaim in the organic-biological matter are laid a good foundation.
Description of drawings
With reference to the accompanying drawings the utility model is described in further detail below.
Fig. 1 is the described a kind of syndeton schematic diagram with high energy oxygen hydrolysis oxidation organic-biological matter real time processing system of the utility model embodiment.
Among the figure:
1, organic-biological matter is pulverized pulper; 2, the slurry pH value is adjusted jar; 3, the micro-nano bubble oxidative degradation of slurry ozone jar; 4, depth hydrolysis's oxidation trough; 5, centrifugal dehydrator; 6, heavy metal filter membrane; 7, micro-nano bubble generator; 8, aeration tank; 9, good oxidation treatment trough; 10, sand filtration purification tank; 11, the feeder of purifying waste water.
The specific embodiment
As shown in Figure 1, the utility model embodiment is described a kind of with high energy oxygen hydrolysis oxidation organic-biological matter real time processing system, comprise organic living beings pulverizing pulper 1, the micro-nano bubble oxidative degradation of the slurry ozone jar 3 oxidation processes groove 9 of becoming reconciled, described organic-biological matter is pulverized pulper 1 and is connected with slurry pH value adjustment jar 2, the slurry pH value is adjusted jars 2 and is connected with the micro-nano bubble oxidative degradation of slurry ozone jar 3, the micro-nano bubble oxidative degradation of slurry ozone jar 3 is connected with depth hydrolysis's oxidation trough 4, depth hydrolysis's oxidation trough 4 is connected with centrifugal dehydrator 5, centrifugal dehydrator 5 is connected with heavy metal filter membrane 6, heavy metal filter membrane 6 is connected with aeration tank 8, described aeration tank 8 is connected with the micro-nano bubble generator 7 oxidation processes groove 9 of becoming reconciled respectively again, good oxidation treatment trough 9 is connected with sand filtration purification tank 10, and sand filtration purification tank 10 connects the feeder 11 of purifying waste water again.
With high energy oxygen hydrolysis oxidation organic-biological matter real-time processing method, use micro-nano bubble technology to make high energy ozone and pure oxygen, concrete steps comprise:
1) pulverize pulper 1 by organic-biological matter organic-biological matter is worn into slurry, rubbish organic-biological matter solid pollution is converted into the mud liquid contamination, and pollution abatement in liquid environment;
2) adjust the pH value of regulating organic-biological chylema body in the jar 2 at the slurry pH value, make slurry be in acid condition, be convenient to the best oxidation effectiveness of ozone performance;
3) use micro-nano bubble generator 7 to make the micro-nano bubble aqueous solution of ozone, make the ozone concentration of the aqueous solution reach the over-saturation state, and make pure oxygen concentration reach over-saturation;
4) by the ozone slurry, the micro-nano bubble oxidative degradation of ozone jar 3 mixes back performance oxidative degradation with Ozone Water with organic-biological chylema body, cracks the biological structure (cell) and the organic compound of organic-biological matter, releasing structure water;
5) by the deep oxidation effect of the micro-nano bubble of pure oxygen, the oxidation Decomposition organic compound reaches stablizes the carbon configuration state;
6) deviate from water in the slurry by centrifugal dehydrator 5, obtain dryly stablizing carbon structure organic matter (moisture 20-40%), eliminate organic biologically active;
7) water deviate from of centrifugal dehydrator 5 is through the micro-nano bubble aeration of pure oxygen, and the pollutant in the oxidative degradation water makes water quality obtain preliminary purification;
8) sewage of oxidative degradation pollutant is eliminated heavy metal through equipotential heavy metal ion polymerization filter membrane 6;
9) water of preliminary purification is by the effect of aerobic bacteria, eliminates water pollutant, reaches the purification of water quality purpose, if the residual contamination owner suspended contaminant (MLSS) at this moment in the water;
10) water after the purification filters through sand filtration purification tank 10, eliminates the suspended contaminant (MLSS) in the water at last, gives off clean water.
In above-mentioned process with high energy oxygen hydrolysis oxidation organic-biological matter real-time processing method, in step 1): the preparation method that described organic-biological matter pulverizing pulper 1 is worn into slurry with organic-biological matter can be that the muddy flesh machine is pulverized or pulverized with the water mill rice-flour noodles machine.
In above-mentioned process with high energy oxygen hydrolysis oxidation organic-biological matter real-time processing method, step 2) to regulate the acid that needs to use can be sulfuric acid, hydrochloric acid or nitric acid to pH value in.
In above-mentioned process with high energy oxygen hydrolysis oxidation organic-biological matter real-time processing method, in step 3): the aeration mode that described micro-nano bubble generator 7 adopts when making the micro-nano bubble of ozone can be that straight tube spiral quickens aeration or the right angle vortex quickens aeration, the aerator that adopts can be single straight tube aeration, also can be the parallel connection of a plurality of straight tube aeration.
In above-mentioned process with high energy oxygen hydrolysis oxidation organic-biological matter real-time processing method, the aeration mode that uses in the step 3) can be the vacuum aeration, also can be the supercharging aeration.
In above-mentioned process with high energy oxygen hydrolysis oxidation organic-biological matter real-time processing method, in step 3): described micro-nano bubble generator 7 ozoniferous source of the gas when making the micro-nano bubble of ozone can be an air, also can be the pure oxygen oxygenerator.
In above-mentioned process with high energy oxygen hydrolysis oxidation organic-biological matter real-time processing method, rapid 4) the ozone carrier that uses in can be an Ozone Water, also can be under the higher condition of slurry water content directly with aerator to the micro-nano bubble of slurry input ozone.
In above-mentioned process with high energy oxygen hydrolysis oxidation organic-biological matter real-time processing method, step 6), 7), the bed mud that produces 9), 10) sends back to step 2 through after the backwash) circulate in utilization.
In above-mentioned process with high energy oxygen hydrolysis oxidation organic-biological matter real-time processing method, in the step 8) granularity of heavy metal polymerization greater than 0.5 micron, the equipotential solution pH value place of use between 11-12, the filter membrane metal selective filter membrane of attaching most importance to.
During concrete the use, organic-biological matter enters pulverizes pulper 1, enter pH value adjustment jar 2 after the pulverizing and carry out the pH value adjustment, slurry enters in the micro-nano bubble oxidative degradation of the slurry ozone jar 3 then, carry out ozone hydrolysis oxidation reaction, enter 4 kinds of depth hydrolysis's oxidation troughs then and carry out the deep oxidation degraded, material was poured in the centrifugal dehydrator 5 and is dewatered after oxidative degradation was finished, dehydration back dry material takes out, carry out recycling, behind the sewage process heavy metal filter membrane 6 filtering heavy metals of deviating from, water enters and carries out aerobic aeration in the aeration tank 8, aerobic aeration uses the micro-nano bubble of micro-nano bubble generator 7 input pure oxygens, sewage has entered and has carried out the aerobic microbiological oxidation processes in the oxidation treatment trough 9 behind the aeration, purifying waste water after the processing enters sand filtration purification tank 10 and carries out filtration treatment, and the clear water that obtains at last enters the feeder 11 of purifying waste water, supply production reuse.
Theoretical foundation with high energy oxygen hydrolysis oxidation organic-biological matter real time processing system is specific as follows:
High energy oxygen is meant the micro-bubble that active oxygen (ozone or pure oxygen) ion cluster with higher-energy and micel constitute, and mainly is present in the water environment.
Use micro-nano bubble generator 7 in water, to import ozone or pure oxygen, in gas-liquid mixed, cause the ionization of portion gas molecule because of dissection to gas, so the particle diameter of 90% above bubble is between 5 nanometers to 50 micron in the bubble that produces through the effect of at a high speed rotation and pressurization gradually, characteristic with charged particle, so ozone that obtains or pure oxygen micro-bubble are actual to be ozone or pure oxygen ion group, it is active oxygen radical, this active oxygen radical has very high energy, and the source of energy is as follows:
1, ionization energy:
Ozone or pure oxygen produce mechanical ionization through cutting, and the generating portion oxonium ion forms active oxygen ion group, mainly comprises (the O of ozone ion group
3 2-, O
3 -), (O of ozone molecule group
3), (O of oxonium ion group
2 2-, O
2 -), (O of oxygen molecule group
2) etc., these active oxygen air mass have very high ionization energy, make the bubble particle produce energy level transition, reach the high level that can produce oxidation at any time, can all materials that touch of oxidation.
2, high speed kinetic energy:
The active oxygen micro-bubble produces ozone or the centrifugal cutting suction of pure oxygen effect through water, generate the air water mixing material, bubble is accompanied by the accelerated motion in the vortex accelerating system of the cutting aqueous solution, since the characteristics of vortex accelerating system be into the water total amount with eject water inventory and equate, and the water inlet diameter is 4 times of the delivery port diameter, so the aqueous solution flow velocity of two delivery ports and instantaneous pressure will reach 8 times of water inlet aqueous solution flow velocity and pressure, speed reaches the 160-320 meter per second, instantaneous pressure reaches 3.2-4MPa, the kinetic energy that the active oxygen micro-bubble is had is very high, be enough in effective propagation path, to break any pollutant and be connected with the chemical bond of pollutant inside with covalent bond between the hydrone and be connected, realize the purification of water quality reduction and the oxidative degradation of pollutant.
Micro-bubble and several typical object of which movement speed contrast:
| Kind | Speed |
| Hydrogen molecule | 1768 meter per seconds |
| Rifle bullet | The 700-1000 meter per second |
| The active oxygen bubble | The 160-320 meter per second |
| Jet plane | 278 meter per seconds |
| High-speed railway | 83 meter per seconds |
3, other energy
Other energy comprises the blast energy that intermolecular energy, bubble break etc.
4, the effect of energy
Multiple energy coexists in the active oxygen micro-bubble, makes the active oxygen bubble have the particle energy of superelevation, and the rank of energy is equivalent to the heat motion of gas molecules energy of gas under 6000-8000 ℃ of condition, reach hundreds of thousands in addition million electron volt more than.These energy can directly destroy the chemical constitution of pollutant in sewage, taking place to play a role the process of guiding and accelerating oxidation reaction before the oxidation reaction.
The motion of active oxygen micro-bubble is caused by the bubble self-energy, bubble makes liquid be heated to the critical condition that chemical reaction can take place at any time in high-speed motion, wherein chemical reaction will be unthinkable with us, can not take place from the speed that the angle of physics is inferred, thereby reach the purpose of oxidative degradation organic-biological matter.
After this treatment process process is finished, obtain stablizing the small organic molecule of carbon structure, these small organic molecules can carry out recycling, can produce organic bio-fertilizer, also can be used for the pyrolytic gasification generating recovery energy wherein.Use high energy oxygen technology to finish the oxidative degradation of organic-biological matter, can be applied to the harmless treatment of house refuse organic-biological matter, can also be used for rubbish from cooking processing and sewage bed mud and handle.
Claims (1)
1. one kind with high energy oxygen hydrolysis oxidation organic-biological matter real time processing system, comprise organic living beings pulverizing pulper (1), the micro-nano bubble oxidative degradation of slurry ozone jar (3) the oxidation processes groove (9) of becoming reconciled, it is characterized in that: described organic-biological matter is pulverized pulper (1) and is connected with slurry pH value adjustment jar (2), the slurry pH value is adjusted jar (2) and is connected with the micro-nano bubble oxidative degradation of slurry ozone jar (3), the micro-nano bubble oxidative degradation of slurry ozone jar (3) is connected with depth hydrolysis's oxidation trough (4), depth hydrolysis's oxidation trough (4) is connected with centrifugal dehydrator (5), centrifugal dehydrator (5) is connected with heavy metal filter membrane (6), heavy metal filter membrane (6) is connected with aeration tank (8), described aeration tank (8) is connected with micro-nano bubble generator (7) the oxidation processes groove (9) of becoming reconciled respectively again, good oxidation treatment trough (9) is connected with sand filtration purification tank (10), and sand filtration purification tank (10) connects the feeder (11) of purifying waste water again.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201488279U CN202079073U (en) | 2011-05-11 | 2011-05-11 | Real-time treatment system using high-energy oxygen for hydrolyzing and oxidizing organic biomass |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201488279U CN202079073U (en) | 2011-05-11 | 2011-05-11 | Real-time treatment system using high-energy oxygen for hydrolyzing and oxidizing organic biomass |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202079073U true CN202079073U (en) | 2011-12-21 |
Family
ID=45339728
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201488279U Expired - Fee Related CN202079073U (en) | 2011-05-11 | 2011-05-11 | Real-time treatment system using high-energy oxygen for hydrolyzing and oxidizing organic biomass |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202079073U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102746034A (en) * | 2012-07-16 | 2012-10-24 | 惠州市神州创宇低碳技术发展有限公司 | Method for producing microorganism luminous energy organic fertilizer by utilizing table/kitchen wastes |
| CN104259177A (en) * | 2014-09-12 | 2015-01-07 | 湖南树林环境科技有限公司 | Method for producing soil conditioner raw material by using kitchen garbage and solid agriculture and forestry wastes |
| CN106277178A (en) * | 2016-08-05 | 2017-01-04 | 北京未名清源环保科技有限公司 | A kind of micro-nano bubble degradation treatment system and method containing organic pollution water body |
| CN106630096A (en) * | 2016-11-09 | 2017-05-10 | 江苏宜星星晨环境工程有限公司 | High-energy-oxygen water purifier system |
| CN108911242A (en) * | 2018-07-23 | 2018-11-30 | 广东上智环保科技有限公司 | A kind of super nano bubble circulation ozone sewage water treatment method and device |
| CN110615550A (en) * | 2019-08-12 | 2019-12-27 | 中原环资科技有限公司 | Water recycling technology for fine garbage sorting process |
-
2011
- 2011-05-11 CN CN2011201488279U patent/CN202079073U/en not_active Expired - Fee Related
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102746034A (en) * | 2012-07-16 | 2012-10-24 | 惠州市神州创宇低碳技术发展有限公司 | Method for producing microorganism luminous energy organic fertilizer by utilizing table/kitchen wastes |
| CN102746034B (en) * | 2012-07-16 | 2014-05-07 | 惠州市神州创宇低碳技术发展有限公司 | Method for producing microorganism luminous energy organic fertilizer by utilizing table/kitchen wastes |
| CN104259177A (en) * | 2014-09-12 | 2015-01-07 | 湖南树林环境科技有限公司 | Method for producing soil conditioner raw material by using kitchen garbage and solid agriculture and forestry wastes |
| CN106277178A (en) * | 2016-08-05 | 2017-01-04 | 北京未名清源环保科技有限公司 | A kind of micro-nano bubble degradation treatment system and method containing organic pollution water body |
| CN106630096A (en) * | 2016-11-09 | 2017-05-10 | 江苏宜星星晨环境工程有限公司 | High-energy-oxygen water purifier system |
| CN108911242A (en) * | 2018-07-23 | 2018-11-30 | 广东上智环保科技有限公司 | A kind of super nano bubble circulation ozone sewage water treatment method and device |
| CN110615550A (en) * | 2019-08-12 | 2019-12-27 | 中原环资科技有限公司 | Water recycling technology for fine garbage sorting process |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101337838B (en) | Combined anaerobic fermentation process for organic solid wastes | |
| CN202079073U (en) | Real-time treatment system using high-energy oxygen for hydrolyzing and oxidizing organic biomass | |
| CN102500604B (en) | Household solid garbage recycling and renewable biological carbon circulating technology | |
| WO2011054298A1 (en) | Method and apparatus for integratedly treating domestic wastewater and organic garbage | |
| CN103240264B (en) | Have the low emission solid organic castoff treatment system of biogas and Activated Carbon Production concurrently | |
| CN202080994U (en) | Harmless and reducing real-time treatment system for sewage and sludge | |
| CN104774044A (en) | Organic waste recycling method and sterilization apparatus used in method | |
| CN106957130B (en) | Treatment method of domestic sewage and organic solid waste | |
| CN204999815U (en) | Vertical spiral discharge's domestic waste fermenting installation | |
| CN102765866B (en) | Method for recycling urban sludge | |
| CN102336508A (en) | Method and system for quickly dehydrating and recycling municipal sewage sludge | |
| CN203946997U (en) | A kind of life in the countryside rubbish and Sewage treatment systems | |
| CN104907321A (en) | Comprehensive garbage treatment method | |
| CN211645010U (en) | Sludge modification system | |
| CN111269729A (en) | Method and system for preparing biochar by co-pyrolysis of sludge and waste tires | |
| CN102755983A (en) | Comprehensive treatment system and method for household wastes | |
| CN109503232A (en) | A kind of garbage fermentation system and method for garbage incinerating power plant | |
| CN202543012U (en) | Fluid sludge treatment device for generating clean combustible gas | |
| CN102924189B (en) | Method for recovering carbon-based ammonium bicarbonate in refuse landfill | |
| CN103723892A (en) | Livestock and poultry wastewater treatment system and treatment method using system | |
| CN110295077A (en) | A kind of regenerated clean fuel and its manufacturing method with oily sludge production | |
| CN212741231U (en) | Municipal sludge and garden waste cooperative recycling treatment system | |
| CN204999814U (en) | Efficient domestic waste fermenting installation | |
| CN211339484U (en) | Urban organic solid waste cooperative treatment system | |
| CN204999816U (en) | Domestic waste fermenting installation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Real-time treatment system using high-energy oxygen for hydrolyzing and oxidizing organic biomass Effective date of registration: 20130426 Granted publication date: 20111221 Pledgee: China Co truction Bank Corp Shenzhen branch Pledgor: Shenzhen Shenzhou Chuangyu Low Carbon Technology Co., Ltd. Registration number: 2013440000006 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20140620 Granted publication date: 20111221 Pledgee: China Co truction Bank Corp Shenzhen branch Pledgor: Shenzhen Shenzhou Chuangyu Low Carbon Technology Co., Ltd. Registration number: 2013440000006 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Real-time treatment system using high-energy oxygen for hydrolyzing and oxidizing organic biomass Effective date of registration: 20141217 Granted publication date: 20111221 Pledgee: China Co truction Bank Corp Shenzhen Nanshan sub branch Pledgor: Shenzhen Shenzhou Chuangyu Low Carbon Technology Co., Ltd. Registration number: 2014440000022 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20160705 Granted publication date: 20111221 |
|
| RINS | Preservation of patent right or utility model and its discharge | ||
| PD01 | Discharge of preservation of patent | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20200705 Granted publication date: 20111221 |
|
| PP01 | Preservation of patent right | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20200705 Granted publication date: 20111221 |
|
| PD01 | Discharge of preservation of patent | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20210105 Granted publication date: 20111221 |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111221 Termination date: 20180511 |