CN103056151B - Kitchen waste oxidizing, deodorizing, inactivating, washing and salt-reducing device - Google Patents
Kitchen waste oxidizing, deodorizing, inactivating, washing and salt-reducing device Download PDFInfo
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- CN103056151B CN103056151B CN201310038148.XA CN201310038148A CN103056151B CN 103056151 B CN103056151 B CN 103056151B CN 201310038148 A CN201310038148 A CN 201310038148A CN 103056151 B CN103056151 B CN 103056151B
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- Prior art keywords
- reactor
- deodorizing
- food waste
- changing food
- deactivation
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- 230000001877 deodorizing effect Effects 0.000 title claims abstract description 26
- 239000010806 kitchen waste Substances 0.000 title abstract 7
- 230000000415 inactivating effect Effects 0.000 title abstract 3
- 230000001590 oxidative effect Effects 0.000 title abstract 3
- 238000005406 washing Methods 0.000 title abstract 3
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 25
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000000463 material Substances 0.000 claims abstract description 21
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 20
- 238000006243 chemical reaction Methods 0.000 claims abstract description 15
- 239000010794 food waste Substances 0.000 claims description 37
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 32
- 238000007254 oxidation reaction Methods 0.000 claims description 20
- 150000003839 salts Chemical class 0.000 claims description 20
- 230000009849 deactivation Effects 0.000 claims description 19
- 230000003647 oxidation Effects 0.000 claims description 19
- 238000004140 cleaning Methods 0.000 claims description 17
- 239000007788 liquid Substances 0.000 claims description 15
- 239000007787 solid Substances 0.000 claims description 7
- BGOFCVIGEYGEOF-UJPOAAIJSA-N helicin Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC1=CC=CC=C1C=O BGOFCVIGEYGEOF-UJPOAAIJSA-N 0.000 claims description 5
- 230000001186 cumulative effect Effects 0.000 claims description 3
- 230000005540 biological transmission Effects 0.000 claims description 2
- 241000894006 Bacteria Species 0.000 abstract description 12
- 238000000034 method Methods 0.000 abstract description 12
- 241000700605 Viruses Species 0.000 abstract description 8
- 244000005700 microbiome Species 0.000 abstract description 5
- 239000002245 particle Substances 0.000 abstract 3
- 208000015181 infectious disease Diseases 0.000 abstract 1
- 230000002458 infectious effect Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 12
- 238000006722 reduction reaction Methods 0.000 description 9
- 238000007599 discharging Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 230000001954 sterilising effect Effects 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 229910001220 stainless steel Inorganic materials 0.000 description 3
- 239000010935 stainless steel Substances 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 244000052616 bacterial pathogen Species 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 238000010612 desalination reaction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- -1 polybag Substances 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 241001270131 Agaricus moelleri Species 0.000 description 1
- 235000019737 Animal fat Nutrition 0.000 description 1
- 238000009303 advanced oxidation process reaction Methods 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 239000006041 probiotic Substances 0.000 description 1
- 235000018291 probiotics Nutrition 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 238000003900 soil pollution Methods 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 235000019871 vegetable fat Nutrition 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
- C10L1/026—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for compression ignition
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/48—Solid fuels essentially based on materials of non-mineral origin on industrial residues and waste materials
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Processing Of Solid Wastes (AREA)
- Fats And Perfumes (AREA)
- Drying Of Solid Materials (AREA)
- Treating Waste Gases (AREA)
- Disinfection, Sterilisation Or Deodorisation Of Air (AREA)
- Liquid Carbonaceous Fuels (AREA)
- Mixers Of The Rotary Stirring Type (AREA)
- Apparatus For Disinfection Or Sterilisation (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
- Catalysts (AREA)
- Treatment Of Sludge (AREA)
- Crushing And Pulverization Processes (AREA)
- Combined Means For Separation Of Solids (AREA)
Abstract
The invention discloses a kitchen waste oxidizing, deodorizing, inactivating, washing and salt-reducing device comprising more than one reactor and a gas-water-material mixer for ozone-water-material mixing, wherein an ozone generator is connected with the mixer; a high-viscosity cam rotor pump is further connected with the mixer; an outlet of the mixer extends into one reactor; an inlet of the high-viscosity cam rotor pump is connected with another reactor; more than one particle active carbon reaction ball is arranged inside each reactor; active carbon particles are arranged inside each particle active carbon reaction ball; and a material outlet is formed in the bottom of the mixer. With the adoption of the kitchen waste oxidizing, deodorizing, inactivating, washing and salt-reducing device provided by the invention, microorganisms, such as bacteria and viruses, in kitchen waste are oxidized, deodorized and inactivated by using ozone; and the kitchen waste is prevented from emitting offensive odor and polluting air. Meanwhile, the microorganisms, such as the bacteria and the viruses, in the kitchen waste are inactivated and are prevented from being spread. Particularly, if the kitchen waste needs to be biochemically treated in the next section, the treatment process is prevented from being interfered by infectious microbes.
Description
Technical field
The present invention discloses a kind of food waste treatment device, more specifically relates to the oxidation of a kind of changing food waste, deodorizing, deactivation, cleaning salt reduction device.
Background technology
The science and technology of utilization of waste as resource; through application for a long time; demonstrate a reason; if be exactly the resource treatment technique single application of discarded object; its consequence will bring larger crisis to environment for human survival; especially the serious problems producing secondary pollution are difficult to control, so the integrated treatment of discarded object has become the trend of current development.The composition of changing food waste is extremely complicated, wherein comprises the material such as sewage, polybag, plastic bottle, useless cloth, putrefactive organism, paper, metal Bottle & Can, broken glass, broken potsherd, animal fat, vegetable fat, primary bacterial body." a hundred flowers blossom " situation is presented in current changing food waste into resources treatment technology Method and process at home and abroad, but be substantially all simple single-item handling, there is no the international environmental protection treatment trend and direction moving towards to turn to integrated treatment from simple process, utilize and dispose, the inevitable attachment in changing food waste may be caused to carry out shifting and disorderly filling out leaving about, cause water and soil pollution, or transfer, not only block urban sewage pipeline, distribute foul odour, cause serious secondary pollution.The single treatment process of changing food waste is worth to consider it is feasible from recycling, but considers from digital preservation earth environment, the people's comprehensive angle that is livable, environment protection, or may be more harm than good.In prior art, Available Material is mainly therefrom obtained to the process of changing food waste and makes feed by biochemical apparatus, but unavoidably can with bacterium, virus and salt etc. in changing food waste, it is along with changing food waste is in processing procedure, if incorrect and effectively process primary bacterium, virus and salt, miscellaneous bacteria will be made to cause having a strong impact on interference biochemical treatment link, and the rate of producing into is low, add the too high of salt, produced commercial feed quality also can be caused to decline.
Summary of the invention
For the above-mentioned changing food waste of the prior art mentioned in processing procedure, easily spread germs, virus, and can because rotten, rotten, give out bad smell, contaminated air, especially in changing food waste biochemical treatment, probiotics can have the shortcoming of significantly interference to the culture propagation added, the invention provides the oxidation of a kind of changing food waste, deodorizing, deactivation, cleaning salt reduction device, it designs through special construction, utilize ozone to be oxidized changing food waste, deodorizing, deactivation is carried out to microorganisms such as bacterium wherein, viruses.
The technical scheme that the present invention solves the employing of its technical problem is: a kind of changing food waste oxidation, deodorizing, deactivation, cleaning salt reduction device, device comprises more than one reactor and the gas of---water---mixing of materials for ozone, water, thing blender, blender is connected with anti-water one-way valve, after one end connecting gas transmission pipe of anti-water one-way valve, connect ozone generating apparatus again, blender is also connected with high viscosity cam follower pump discharge, the outlet of blender is stretched in a reactor, the entrance of high viscosity lobed rotor pump is connected with another reactor, more than one grain active carbon reaction sphere is provided with in reactor, grain active carbon is provided with in grain active carbon reaction sphere, reactor bottom is provided with material outlet.
The technical scheme that the present invention solves the employing of its technical problem further comprises:
The cumulative volume of described grain active carbon accounts for 15% of grain active carbon reaction sphere sphere cavity volume---and 98%.
Described reactor head is provided with automatic exhaust steam valve, automatic exhaust steam valve is connected with ozone and destroys device.
Described reactor bottom is provided with semicircle end socket, and material outlet is arranged on semicircle end socket.
In described reactor, reactor is foremost provided with inclined-plane ribbon conveyer, and the reactor of rear end is provided with height of water level and regulates pipeline.
Described material outlet place is connected with solid, liquid separator.
Described solid, liquid separator comprises shell and the netted staving that tilts, the netted staving that tilts is arranged in the enclosure, the netted staving that tilts coordinates speed changer to drive rotation by motor, the netted staving front end that tilts is provided with the above mesh of a row, tilt in netted staving and be provided with the spiral helicine ribbon being connected to netted inner wall of barrel, outer casing bottom is provided with water butt.
Described spiral helicine ribbon accounts for the total length of netted staving.
Described shell is equipped with form.
Manhole is equipped with in described reactor side.
The invention has the beneficial effects as follows: utilize the present invention to adopt ozone and water body are oxidized changing food waste, deodorizing, desalination, simultaneously, deactivation can be carried out to microorganisms such as the bacterium in changing food waste, viruses, ensure that changing food waste does not disturb by miscellaneous bacteria in biochemical treatment operation.
Below in conjunction with the drawings and specific embodiments, the present invention will be further described.
Accompanying drawing explanation
Fig. 1 is wet type advanced oxidation of the present invention deodorizing, sterilizing, cleaning salt reduction apparatus structure schematic diagram.
Fig. 2 is solid, liquid cyclone separator arrangement schematic diagram in the present invention.
In figure, 1-reactor, 2-semicircle end socket, 3-inclined-plane ribbon conveyer, 4-flat-top end socket, 5-automatic exhaust steam valve, 6-ozone destroys device, the online automatic liquid surface control watch-dog of 7-, 8-grain active carbon reaction sphere, 9-blender, 10-high viscosity lobed rotor pump, the anti-water one-way valve of 11-, 12-motor, the deodorizing of 13-wet type advanced oxidation, sterilizing, cleaning salt reduction device, 14-manhole, 15, 15A-discharging opening, 16-height of water level controls pipeline, 17-gas, water, thing mixture conveyance conduit, 18-gas outlet pipe section, 19-ozone input pipeline section, 20-ozone generator, 21-pneumatic ball valve, 22-high viscosity cam follower pump discharge, 23-solid-liquid separator shell, 24-form, the netted staving of 25-, 26-ribbon water conservancy diversion discharging opening, 27-water butt.
Detailed description of the invention
The present embodiment is the preferred embodiment for the present invention, and other its principles all are identical with the present embodiment or approximate with basic structure, all within scope.
The present invention mainly utilizes ozone gas to carry out sterilization and cleaning to changing food waste in water body, this device is divided into more than one reactor 1, and each reactor 1 is interconnected by pump and pipeline and is circulated in each reactor 1, the quantity of concrete reactor 1, can set according to actual needs.
By with the structure of a concrete reactor 1, the present invention is specifically described below.Please refer to accompanying drawing 1, reactor 1 is cylindrical, for stainless steel cavity structure, reactor 1 bottom is semicircle end socket 2, and the top of reactor 1 is semicircle or flat-top end socket 4, and the top end socket 4 of reactor 1 is provided with automatic exhaust steam valve 5, automatic exhaust steam valve 5 is connected with ozone and destroys device 6, gas in reactor 1 is got rid of in ozone destruction device 6 by automatic exhaust steam valve 5, destroys ozone remaining in device 6 pairs of gases and removes, then discharged by gas outlet pipe section 18 by ozone.In the present embodiment, the porch of reactor 1 is connected with inclined-plane ribbon conveyer 3, the changing food waste discarded object of sorting is sent in the deodorizing of wet type advanced oxidation, sterilizing, cleaning salt reduction device 13 by inclined-plane ribbon conveyer 3, inclined-plane ribbon conveyer 3 in a tubular form, inside is provided with conveying ribbon, by carrying the rotation of ribbon, material is sent into reactor 1.The inner chamber body inner rim of reactor 1 is installed with more than one grain active carbon reaction sphere 8, its position is loaded on the upper position in reactor 1 inner chamber body, grain active carbon reaction sphere 8 is the netted shell of stainless steel, grain active carbon is wrapped in the netted enclosure of stainless steel, in the present embodiment, the cumulative volume of grain active carbon accounts for 15% of grain active carbon reaction sphere 8 sphere cavity volume---and 98%, the use in conjunction of grain active carbon reaction sphere and ozone, can make ozone in liquid state, accelerate to be converted into the effect of hydroxyl radical free radical, reach and promote ozone to the artificial pressure deactivation of bacterium in water and deodorizing speed.In the present embodiment, reactor 1 inner cavity top is also equipped with online automatic liquid surface control watch-dog 7, for the liquid level in monitoring reactor 1, online automatic liquid surface control watch-dog 7 can adopt liquid sensor to realize, and by the height of water level of another reactor 1 control pipeline 16 to, row, liquid level is adjusted.
In the present embodiment, the shell of reactor 1 is also provided with the gas of---water---mixing of materials for ozone, water, thing blender 9.Blender 9 is threeway connection, the inner chamber of reactor 1 is led to by connecting pipe 17 in its one end, the other end is communicated with the outlet 22 of high viscosity lobed rotor pump 12, the center-side of blender 9 is connected with air inlet, air inlet is connected to anti-water one-way valve 11 place, the gas that ozone generator 20 provides is entered by appendix 19 and by anti-water one-way valve 11, enter in blender 9 and water, thing powerful mixing, the mixture of---changing food waste---ozone that makes water with this is transported to another reactor 1 by the high viscosity lobed rotor pump 10 be located in the circulating line of reactor 1 bottom again, and form a process moved in circles between two reactors, control the mixing continuous print oxidization time of material.
Said structure is front portion structure of the present invention, the present invention also includes rear structure, the rear portion of advanced oxidation deodorizing, sterilizing, salt reduction part device is solid, liquid separator, incorporated by reference to referring to accompanying drawing 2, in the present embodiment, separator is made up of the netted staving 24 that tilts, separator front end is connected to the discharging opening 15A place of the semicircle end socket 2 bottom reactor 1, staving 24 is provided with arranges mesh more, in the present embodiment, mesh diameter is 3-8mm, is provided with shell 22 outside staving 24, form 23 is equipped with in shell 22 side, for watching staving 24 inner case.Be provided with bottom shell 22 and water butt 25 is installed, for accepting the water that netted staving 24 leaks down, in inclination staving 24, total length is equipped with water conservancy diversion ribbon and leads to discharging opening 26, namely in netted staving 24 total length of inclination, spiral helicine ribbon is housed, by ribbon, material is derived, tilt the rotational power of netted staving 24, comes from alternating current generator and coordinate speed changer to drive, not shown in FIG..
The present invention in use, water and changing food waste mixture are dropped in reactor 1 by ramp conveyor 3, the ratio of its changing food waste mixture and water volume is 5:7, in mobility, utilize high viscosity lobed rotor pump 10 to be circulated in incessantly in each reactor and outer between, and at water---add ozone gas in gas blender 9, with water---changing food waste material Forced Mixing, ozone concentration in mixed material is 10g/T---15g/T, mixed material utilizes to be circulated in reactor and reacts as advanced oxidation with outer run duration, all times is 5min---15min, because ozone moment in water, reduction reaction occurred, and chain reaction is caused under the assistance reagentia of activated carbon reaction sphere, accelerate ozone is converted into hydroxy radical, be similar to O
3/ H
2o
2or O
3the advanced oxidation processes of/UV, produces antozone and the hydroxyl OH of strong oxidation, manually forces deactivation and deodorizing and remove sodium chloride material to the pathogenic bacteria in changing food waste.When changing food waste is after workshop section bacterium being carried out to artificial deactivation and deodorizing completes, open reactor discharging opening 15A bottom valve, utilize high viscosity lobed rotor pump to input in solid, liquid separator and dewater.
Utilize the present invention, can adopt that ozone is oxidized changing food waste, deodorizing, desalination, prevent it from distributing bad smell, contaminated air, simultaneously, deactivation can be carried out to microorganisms such as the bacterium in changing food waste, viruses, prevent it from disseminating, if especially when next workshop section needs to carry out biochemical treatment to changing food waste, ensure that processing procedure is not disturbed by miscellaneous bacteria.
Claims (9)
1. a changing food waste oxidation, deodorizing, deactivation, cleaning salt reduction device, it is characterized in that: described device comprises more than one reactor (1) and the gas of---water---mixing of materials for ozone, water, thing blender (9), described reactor (1) top is provided with automatic exhaust steam valve (5), automatic exhaust steam valve (5) is connected with ozone and destroys device (6), blender (9) is connected with anti-water one-way valve (11), after one end connecting gas transmission pipe (19) of anti-water one-way valve (11), connect ozone generating apparatus (20) again, blender (9) is also connected with high viscosity cam follower pump discharge (22), the outlet of blender (9) is stretched in a reactor (1), the entrance of high viscosity lobed rotor pump (10) is connected with another reactor (1), more than one grain active carbon reaction sphere (8) is provided with in reactor (1), grain active carbon reaction sphere is provided with grain active carbon in (8), reactor (1) bottom is provided with material outlet (15, 15A).
2. changing food waste oxidation according to claim 1, deodorizing, deactivation, cleaning salt reduction device, is characterized in that: the cumulative volume of described grain active carbon accounts for 15% of grain active carbon reaction sphere (8) sphere cavity volume---98%.
3. changing food waste oxidation according to claim 1 and 2, deodorizing, deactivation, cleaning salt reduction device, is characterized in that: described reactor (1) bottom is provided with semicircle end socket (2), and material outlet (15,15A) is arranged on semicircle end socket (2).
4. changing food waste oxidation according to claim 1 and 2, deodorizing, deactivation, cleaning salt reduction device, it is characterized in that: in described reactor (1), reactor (1) is foremost provided with inclined-plane ribbon conveyer (3), and the reactor of rear end (1) is provided with height of water level and regulates pipeline (16).
5. changing food waste oxidation according to claim 1 and 2, deodorizing, deactivation, cleaning salt reduction device, is characterized in that: material outlet (15A) place of the reactor of rear end is connected with solid, liquid separator.
6. changing food waste oxidation according to claim 5, deodorizing, deactivation, cleaning salt reduction device, it is characterized in that: described solid, liquid separator comprises shell (22) and the netted staving (24) that tilts, the netted staving (24) that tilts is arranged in shell (22), the netted staving (24) that tilts coordinates speed changer to drive rotation by motor, netted staving (24) front end that tilts is provided with the above mesh of a row, tilt in netted staving (24) and be provided with the spiral helicine ribbon being connected to netted inner wall of barrel, shell (22) bottom is provided with water butt (25).
7. changing food waste oxidation according to claim 6, deodorizing, deactivation, cleaning salt reduction device, is characterized in that: described spiral helicine ribbon accounts for the total length of netted staving (24).
8. changing food waste oxidation according to claim 6, deodorizing, deactivation, cleaning salt reduction device, is characterized in that: described shell (22) is equipped with form (23).
9. changing food waste oxidation according to claim 1 and 2, deodorizing, deactivation, cleaning salt reduction device, is characterized in that: manhole (14) is equipped with in described reactor (1) side.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201310038148.XA CN103056151B (en) | 2012-11-23 | 2013-01-31 | Kitchen waste oxidizing, deodorizing, inactivating, washing and salt-reducing device |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
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CN2012104812748 | 2012-11-23 | ||
CN201210481274.8 | 2012-11-23 | ||
CN201210481274 | 2012-11-23 | ||
CN201310038148.XA CN103056151B (en) | 2012-11-23 | 2013-01-31 | Kitchen waste oxidizing, deodorizing, inactivating, washing and salt-reducing device |
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CN103056151A CN103056151A (en) | 2013-04-24 |
CN103056151B true CN103056151B (en) | 2015-07-15 |
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Family Applications (17)
Application Number | Title | Priority Date | Filing Date |
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CN201310037944.1A Expired - Fee Related CN103056022B (en) | 2012-11-23 | 2013-01-31 | Combined screening system of kitchen wastes |
CN201310038171.9A Expired - Fee Related CN103084049B (en) | 2012-11-23 | 2013-01-31 | Plasma photocatalyst anion air deodorization, sterilizing unit |
CN201310037324.8A Expired - Fee Related CN103072726B (en) | 2012-11-23 | 2013-01-31 | Plastic bag segmenting and lacerating device for holding kitchen wastes |
CN201310038148.XA Expired - Fee Related CN103056151B (en) | 2012-11-23 | 2013-01-31 | Kitchen waste oxidizing, deodorizing, inactivating, washing and salt-reducing device |
CN201310038212.4A Expired - Fee Related CN103060100B (en) | 2012-11-23 | 2013-01-31 | Distillation-free biodiesel production method and system |
CN201310038136.7A Expired - Fee Related CN103115477B (en) | 2012-11-23 | 2013-01-31 | Automatic discharging multi-stage drying device |
CN2013200552991U Withdrawn - After Issue CN203124395U (en) | 2012-11-23 | 2013-01-31 | Oxidization, deodorization, inactivation, cleaning and desaltation device for kitchen waste |
CN2013200551768U Expired - Fee Related CN203124394U (en) | 2012-11-23 | 2013-01-31 | Material selecting device |
CN2013200551772U Expired - Fee Related CN203128526U (en) | 2012-11-23 | 2013-01-31 | Distillation-free biodiesel production system |
CN201310038166.8A Expired - Fee Related CN103055650B (en) | 2012-11-23 | 2013-01-31 | Exhaust treatment system |
CN2013200542519U Withdrawn - After Issue CN203124392U (en) | 2012-11-23 | 2013-01-31 | Integrated equipment for comprehensive treatment of kitchen waste |
CN201310038156.4A Expired - Fee Related CN103074131B (en) | 2012-11-23 | 2013-01-31 | Preparation method and device of oxygen-enriched microemulsion mixed biodiesel |
CN201310038186.5A Expired - Fee Related CN103056152B (en) | 2012-11-23 | 2013-01-31 | biochemical fermentation method and device |
CN201320054411XU Withdrawn - After Issue CN203316248U (en) | 2012-11-23 | 2013-01-31 | Combined screening system for kitchen waste |
CN2013200551166U Withdrawn - After Issue CN203124393U (en) | 2012-11-23 | 2013-01-31 | Biochemical fermentation device |
CN201310038252.9A Expired - Fee Related CN103071666B (en) | 2012-11-23 | 2013-01-31 | Integrated equipment for omnibearing treatment of kitchen garbage and production method of products |
CN2013200551753U Withdrawn - After Issue CN203323492U (en) | 2012-11-23 | 2013-01-31 | Automatic discharge multi-stage drying device |
Family Applications Before (3)
Application Number | Title | Priority Date | Filing Date |
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CN201310037944.1A Expired - Fee Related CN103056022B (en) | 2012-11-23 | 2013-01-31 | Combined screening system of kitchen wastes |
CN201310038171.9A Expired - Fee Related CN103084049B (en) | 2012-11-23 | 2013-01-31 | Plasma photocatalyst anion air deodorization, sterilizing unit |
CN201310037324.8A Expired - Fee Related CN103072726B (en) | 2012-11-23 | 2013-01-31 | Plastic bag segmenting and lacerating device for holding kitchen wastes |
Family Applications After (13)
Application Number | Title | Priority Date | Filing Date |
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CN201310038212.4A Expired - Fee Related CN103060100B (en) | 2012-11-23 | 2013-01-31 | Distillation-free biodiesel production method and system |
CN201310038136.7A Expired - Fee Related CN103115477B (en) | 2012-11-23 | 2013-01-31 | Automatic discharging multi-stage drying device |
CN2013200552991U Withdrawn - After Issue CN203124395U (en) | 2012-11-23 | 2013-01-31 | Oxidization, deodorization, inactivation, cleaning and desaltation device for kitchen waste |
CN2013200551768U Expired - Fee Related CN203124394U (en) | 2012-11-23 | 2013-01-31 | Material selecting device |
CN2013200551772U Expired - Fee Related CN203128526U (en) | 2012-11-23 | 2013-01-31 | Distillation-free biodiesel production system |
CN201310038166.8A Expired - Fee Related CN103055650B (en) | 2012-11-23 | 2013-01-31 | Exhaust treatment system |
CN2013200542519U Withdrawn - After Issue CN203124392U (en) | 2012-11-23 | 2013-01-31 | Integrated equipment for comprehensive treatment of kitchen waste |
CN201310038156.4A Expired - Fee Related CN103074131B (en) | 2012-11-23 | 2013-01-31 | Preparation method and device of oxygen-enriched microemulsion mixed biodiesel |
CN201310038186.5A Expired - Fee Related CN103056152B (en) | 2012-11-23 | 2013-01-31 | biochemical fermentation method and device |
CN201320054411XU Withdrawn - After Issue CN203316248U (en) | 2012-11-23 | 2013-01-31 | Combined screening system for kitchen waste |
CN2013200551166U Withdrawn - After Issue CN203124393U (en) | 2012-11-23 | 2013-01-31 | Biochemical fermentation device |
CN201310038252.9A Expired - Fee Related CN103071666B (en) | 2012-11-23 | 2013-01-31 | Integrated equipment for omnibearing treatment of kitchen garbage and production method of products |
CN2013200551753U Withdrawn - After Issue CN203323492U (en) | 2012-11-23 | 2013-01-31 | Automatic discharge multi-stage drying device |
Country Status (6)
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KR (1) | KR20150105299A (en) |
CN (17) | CN103056022B (en) |
HK (9) | HK1180714A1 (en) |
RU (1) | RU2015123832A (en) |
SG (1) | SG11201503980RA (en) |
WO (10) | WO2014079169A1 (en) |
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