CN106994460A - The odor removal of organic waste microbial processor - Google Patents
The odor removal of organic waste microbial processor Download PDFInfo
- Publication number
- CN106994460A CN106994460A CN201710205619.XA CN201710205619A CN106994460A CN 106994460 A CN106994460 A CN 106994460A CN 201710205619 A CN201710205619 A CN 201710205619A CN 106994460 A CN106994460 A CN 106994460A
- Authority
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- Prior art keywords
- blade
- linkage section
- organic waste
- foul smell
- stir storehouse
- 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.)
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- 239000010815 organic waste Substances 0.000 title claims abstract description 32
- 230000000813 microbial effect Effects 0.000 title claims abstract description 18
- 238000003756 stirring Methods 0.000 claims abstract description 59
- 239000010813 municipal solid waste Substances 0.000 claims abstract description 49
- 238000006243 chemical reaction Methods 0.000 claims abstract description 30
- 238000004332 deodorization Methods 0.000 claims abstract description 22
- 239000000463 material Substances 0.000 claims abstract description 18
- 238000001179 sorption measurement Methods 0.000 claims abstract description 16
- 238000009423 ventilation Methods 0.000 claims abstract description 16
- 238000001914 filtration Methods 0.000 claims abstract description 14
- 238000001816 cooling Methods 0.000 claims abstract description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical class [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 16
- 230000007246 mechanism Effects 0.000 claims description 14
- 239000011248 coating agent Substances 0.000 claims description 12
- 238000000576 coating method Methods 0.000 claims description 12
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- 238000007254 oxidation reaction Methods 0.000 claims description 10
- 230000003197 catalytic effect Effects 0.000 claims description 8
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 claims description 8
- 229910052753 mercury Inorganic materials 0.000 claims description 8
- 230000002787 reinforcement Effects 0.000 claims description 7
- 229910001220 stainless steel Inorganic materials 0.000 claims description 4
- 239000010935 stainless steel Substances 0.000 claims description 4
- 239000007787 solid Substances 0.000 claims description 2
- 238000007493 shaping process Methods 0.000 claims 1
- 238000013517 stratification Methods 0.000 claims 1
- 238000013461 design Methods 0.000 abstract description 4
- 230000008901 benefit Effects 0.000 abstract description 3
- 238000000354 decomposition reaction Methods 0.000 description 9
- 239000007789 gas Substances 0.000 description 9
- 238000000034 method Methods 0.000 description 9
- 230000000694 effects Effects 0.000 description 8
- 230000008569 process Effects 0.000 description 8
- 241000894006 Bacteria Species 0.000 description 7
- 239000000428 dust Substances 0.000 description 6
- 230000000875 corresponding effect Effects 0.000 description 5
- 244000005700 microbiome Species 0.000 description 5
- 239000008187 granular material Substances 0.000 description 4
- 239000002912 waste gas Substances 0.000 description 4
- 230000001877 deodorizing effect Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- LSDPWZHWYPCBBB-UHFFFAOYSA-N Methanethiol Chemical compound SC LSDPWZHWYPCBBB-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 235000021190 leftovers Nutrition 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 102000004169 proteins and genes Human genes 0.000 description 2
- 108090000623 proteins and genes Proteins 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 150000003384 small molecules Chemical class 0.000 description 2
- DMIUGJLERMOBNT-UHFFFAOYSA-N 4-amino-n-(3-methoxypyrazin-2-yl)benzenesulfonamide;5-[(3,4,5-trimethoxyphenyl)methyl]pyrimidine-2,4-diamine Chemical compound COC1=NC=CN=C1NS(=O)(=O)C1=CC=C(N)C=C1.COC1=C(OC)C(OC)=CC(CC=2C(=NC(N)=NC=2)N)=C1 DMIUGJLERMOBNT-UHFFFAOYSA-N 0.000 description 1
- 241000186046 Actinomyces Species 0.000 description 1
- 241000251468 Actinopterygii Species 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 241000192700 Cyanobacteria Species 0.000 description 1
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 241000206602 Eukaryota Species 0.000 description 1
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- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000009933 burial Methods 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 238000009298 carbon filtering Methods 0.000 description 1
- 230000001925 catabolic effect Effects 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000002361 compost Substances 0.000 description 1
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- 230000002079 cooperative effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 235000013601 eggs Nutrition 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
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- 230000002708 enhancing effect Effects 0.000 description 1
- 210000002615 epidermis Anatomy 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
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- 238000009434 installation Methods 0.000 description 1
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- 238000012986 modification Methods 0.000 description 1
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- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000003895 organic fertilizer Substances 0.000 description 1
- 239000011368 organic material Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000001850 reproductive effect Effects 0.000 description 1
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- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
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- 239000011573 trace mineral Substances 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 210000001835 viscera Anatomy 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE
- 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
- B09B2101/00—Type of solid waste
- B09B2101/02—Gases or liquids enclosed in discarded articles, e.g. aerosol cans or cooling systems of refrigerators
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/30—Particle separators, e.g. dust precipitators, using loose filtering material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/90—Odorous compounds not provided for in groups B01D2257/00 - B01D2257/708
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/91—Bacteria; Microorganisms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/80—Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
- B01D2259/804—UV light
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/80—Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
- B01D2259/818—Employing electrical discharges or the generation of a plasma
Abstract
The present invention relates to the odor removal of organic waste microbial processor, including processor body;The processor body is provided with sort operation platform;Material pour spout is provided with the sort operation platform;Stir storehouse and pulverizer are provided with processor body, the charging aperture of stir storehouse is corresponding with the material pour spout position of sort operation platform;Pulverizer is located between material pour spout bottom and the charging aperture of stir storehouse;It is provided with the top of stir storehouse in aeration-cooling device, stir storehouse and is laid with agitating device;Stir storehouse side wall, which is connected with blast pipe, blast pipe, is connected with rubbish deodorization purifier, and rubbish deodorization purifier is fixedly arranged on processor body;The present invention is by by cleverly setting and being reasonably laid out, taking full advantage of rubbish filtering layer, foul smell adsorption reaction chamber and foul smell ventilating layer;Complete deodorization and ventilation function well, design science, rationally.
Description
Technical field
The invention belongs to Domestic garbage treatment equipment technical field, more particularly, to removing for organic waste microbial processor
Smelly device.
Background technology
Organic waste micropopulation be a class complex microorganism include prokaryotes (bacterium, actinomyces and cyanobacteria),
Eucaryote (fungi and microalgae).It has the features such as small volume, surface area are big, reproductive capacity is surprising, can constantly and surrounding
Environment quickly carries out mass exchange, and to the strong adaptability of pollutant, the high effective microbial community for organic garbage treatment is multiple
With flora, flora can discharge substantial amounts of catabolic enzyme, can the organic matter such as efficient-decomposition protein, fat, cellulose, while deodorization
Flora can suppress the stink produced in organic waste decomposable process, it is to avoid produce air pollution;Due to high effective microbial community
Efficient-decomposition ability, organic waste is decomposed with the speed of decades of times faster than Traditional compost, and degree of decomposition is higher.
At present, modern social economy is developed rapidly, and rhythm of life is constantly accelerated, with the improvement of people ' s living standards and
The quickening of urbanization process, the yield of China's domestic waste also continues to increase.Garbage is accounted in house refuse
37%-62%, has become the major pollutants of city appearance environment.The main such as leftovers leftovers of garbage, the dish leaf trimed vegetables for cooking, dish root,
Epidermis or internal organ that flesh of fish eggs etc. are washed etc., the composition of these house refuses are mainly with starch, protein, and fat is
Lead, also nitrogen, phosphorus, potassium, the various trace elements such as calcium, the discarded object that these kitchen organic refuses are available with is used to it
Suitable processing method, can be effectively converted into a considerable number of organic fertilizer.
Existing house refuse is mainly crushed by garbage disposer, is covered after being shipped after stirring by refuse collector
Bury, the rubbish after burial in the environment can be by biological bacterium natural decomposition, but in rubbish crushing or whipping process, can divide
Solution produces the foul gas such as ammonia, hydrogen sulfide, methyl mercaptan, lower fatty acid, amine, and the foul gas of generation can pass through garbage disposal
The discharging opening of machine is excluded into air, and then pollutes environment, and existing deodorizing device and deodorizing method are not simple efficient enough, deodorization
Effect is unsatisfactory;Meanwhile, during deodorizing device is carried out to organic waste, certain noise can be caused, for building ring
Noise pollution is caused in border, and influence workman's is healthy.
For problem above, therefore, it is necessary to make improvements.
The content of the invention
The present invention is that there is provided a kind of simple in construction, easy to use, deodorization effect in order to overcome above-mentioned defect of the prior art
It is really good, while the odor removal of the organic waste microbial processor of noise pollution can also simultaneously be reduced in deodorization.
In order to reach object above, the technical solution adopted in the present invention is:The deodorization of organic waste microbial processor
Device, including processor body;The processor body is provided with sort operation platform;Material is provided with the sort operation platform
Pour spout;Stir storehouse and pulverizer, the charging aperture of stir storehouse and the material pour spout of sort operation platform are provided with processor body
Position is corresponding;Pulverizer is located between material pour spout bottom and the charging aperture of stir storehouse;Ventilation is provided with the top of stir storehouse
Agitating device is laid with heat sink, stir storehouse;Stir storehouse side wall, which is connected with blast pipe, blast pipe, is connected with rubbish deodorization
Purifier, rubbish deodorization purifier is fixedly arranged on processor body.
As a preferred embodiment of the present invention, the rubbish deodorization purifier includes housing, in housing under
The supreme rubbish filtering layer laid successively, foul smell adsorption reaction chamber and foul smell ventilating layer;The housing is made of stainless steel;Rubbish
Gap is respectively kept between filter layer, foul smell adsorption reaction chamber and foul smell ventilating layer;The rubbish filtering layer is activated carbon filtering
Activated carbon is filled with layer, activated carbon filter layer;The foul smell adsorption reaction intracavitary be arranged in parallel multigroup reaction polar plate, and foul smell is inhaled
Multiple ultraviolet mercury lamps, the power supply of reaction polar plate and ultraviolet mercury lamp respectively with hull outside are uniformly installed on reaction enclosure chamber surrounding inwall
It is connected, and surrounding inwall coating catalytic oxidation coating.
As a preferred embodiment of the present invention, the foul smell ventilating layer includes being located at logical with certain knuckle in housing
Wind passage;The vent passages are formed by connecting by least two pieces identicals ventilation wallboards;Vent passages lower end is connected with for fixing
The reinforcement of ventilation wallboard.
As a preferred embodiment of the present invention, the ventilation wallboard is connected by the first linkage section, the second linkage section and the 3rd
Connect section to be formed by fixedly connecting, be integrally formed;First linkage section is vertical with the top of housing to be connected, and the 3rd linkage section hangs down with reinforcement
Direct-connected to connect, the second linkage section is oblique, for connecting the first linkage section and the 3rd linkage section;Second linkage section and the 3rd
The equal length of linkage section;The length of first linkage section is the 1/2 of the 3rd connection segment length;Second linkage section and first connects
Section and the 3rd linkage section is connect to tilt in 30 °~60 ° of angle.
As a preferred embodiment of the present invention, the case top is provided with discharge duct, and discharge duct lower end is installed
There is trumpet type suction opeing, trumpet type suction opeing upper end is provided with air exhauster.
As a preferred embodiment of the present invention, the exhaust outlet of the blast pipe is relative with the position of aeration-cooling device
Should.
As a preferred embodiment of the present invention, the agitating device includes main shaft, agitating shaft and is socketed on agitating shaft
Some stirring vane mechanisms;Agitating shaft is socketed on main shaft, the stirring vane mechanism include connecting tube, blade fix bar and
Blade;One end of the blade fix bar is fixedly connected with connecting tube, and the other end of blade fix bar is used to fix blade;It is some
Connecting tube is equidistantly socketed on agitating shaft, and adjacent blades fix bar has identical angle of inclination along agitating shaft circumferencial direction;Most
Gap is left between the blade in left side and the exhaust outlet of blast pipe, and blast pipe is located at the upper end of blade.
As a preferred embodiment of the present invention, the blade and blade fix bar vertical runs, blade and agitating shaft it
Between angle of inclination be 30 °~45 °.
As a preferred embodiment of the present invention, the connecting tube is detachably socketed on agitating shaft, and connecting tube is provided with
Two symmetrical positioning holes, corresponding, agitating shaft is provided with the locating slot being adapted with positioning hole, and positioning hole is with determining
Position groove is bolted.
As a preferred embodiment of the present invention, the connection of the connecting tube and blade fix bar goes out to be installed with supporting plate,
Supporting plate is symmetrically laid in connecting tube both sides, and supporting plate is located at two positioning hole centre positions.
The beneficial effects of the invention are as follows:
1. the present invention is combined by agitating device, aeration-cooling device and rubbish deodorization purifier, cooling can be both played
The effect of ventilation, can play the effect of dust suction again, by cleverly setting and being reasonably laid out, take full advantage of rubbish filtering
Layer, foul smell adsorption reaction chamber and foul smell ventilating layer;Deodorization and ventilation function are completed well, foul smell is effectively avoided and causes
The drawbacks of environmental pollution, design science, rationally.
2. agitating device is by setting some equidistant stirring vane mechanisms being laid on agitating shaft, with agitating shaft
Rotate, drive blade to decompose the organic waste decomposed in cabin, improve the stirring efficiency of rubbish so that the volatilization of refuse odor
Faster, purification refuse odor is more efficient.
3. by ultraviolet catalytic, catalysis oxidation, the cooperative effect of electric field, stink substance, harmful microorganism in waste gas,
Bacterium etc. is effectively thoroughly removed;By the waste gas of this reactor for treatment, foul gas reaches more than 99% except rate, is harmful to
Microorganism, the clearance of bacterium reach 99.5%, and the clearance of dust granules reaches 97.8%.
Brief description of the drawings
Fig. 1 is structural representation of the embodiment of the present invention;
Fig. 2 is agitating device structural representation of the embodiment of the present invention;
Reference in figure:Processor body 1, sort operation platform 2, material pour spout 3, pulverizer 4, stir storehouse 5, agitating device
6, main shaft 61, agitating shaft 62, stirring vane mechanism 63, connecting tube 63-1, positioning hole 63-1-1, blade fix bar 63-2, blade
63-3, left bank blade 63-3-1, right bank blade 63-3-2, connect blade 63-3-3, through hole 63-3-4, supporting plate 63-4,
Aeration-cooling device 7, rubbish deodorization purifier 8, blast pipe 9, housing 10, rubbish filtering layer 11, foul smell adsorption reaction chamber 12,
Foul smell ventilating layer 13, reaction polar plate 14, ultraviolet mercury lamp 15, power supply 16, catalytic oxidation coating 17, vent passages 18, ventilation
Wallboard 19, the first linkage section 19-1, the second linkage section 19-2, the 3rd linkage section 19-3, reinforcement 20, discharge duct 21, loudspeaker
Type suction opeing 22, air exhauster 23.
Embodiment
The embodiment of the present invention is elaborated below in conjunction with the accompanying drawings.
Embodiment:As shown in Figure 1-2, including processor body 1;The processor body 1 is provided with sort operation platform 2;
Material pour spout 3 is provided with the sort operation platform 2;Stir storehouse 5 and pulverizer 4, stir storehouse 5 are provided with processor body 1
Charging aperture it is corresponding with the position of material pour spout 3 of sort operation platform 2;Pulverizer 4 is located at the bottom of material pour spout 3 and stirring
Between the charging aperture in storehouse 5;The top of stir storehouse 5, which is provided with aeration-cooling device 7, stir storehouse 5, is laid with agitating device 6;Stirring
The side wall of storehouse 5, which is connected with blast pipe 9, blast pipe 9, is connected with rubbish deodorization purifier 8, and rubbish deodorization purifier 8 is fixedly arranged on
On processor body 1;
The present invention is combined by agitating device 6, aeration-cooling device 7 and rubbish deodorization purifier 8, can both play cooling
The effect of ventilation, can play the effect of dust suction again, by cleverly setting and being reasonably laid out, take full advantage of rubbish filtering
Layer, foul smell adsorption reaction chamber and foul smell ventilating layer;Deodorization and ventilation function are completed well, foul smell is effectively avoided and causes
The drawbacks of environmental pollution, design science, rationally.
Rubbish deodorization purifier 8 includes housing 10, the rubbish filtering layer laid successively from the bottom to top in housing 10
11, foul smell adsorption reaction chamber 12 and foul smell ventilating layer 13;The housing 7 is made of stainless steel;Rubbish filtering layer 11, foul smell absorption
Gap is respectively kept between reaction chamber 12 and foul smell ventilating layer 13;The rubbish filtering layer 11 is activated carbon filter layer, activated carbon
Activated carbon is filled with filter layer;Be arranged in parallel multigroup reaction polar plate 14 in the foul smell adsorption reaction chamber 12, and foul smell absorption is anti-
Answer and multiple ultraviolet mercury lamps 15 be uniformly installed on the surrounding inwall of chamber 12, reaction polar plate 14 and ultraviolet mercury lamp 15 respectively with outside housing 10
Power supply 16 be connected, and surrounding inwall coating catalytic oxidation coating 17;Waste gas enters Stainless Steel Shell 10 by blast pipe 9
Inside, intercepts dust granules in gas, to reduce dust granules to subsequent reactions pole by the activated carbon in rubbish filtering layer 11
The damage of plate 14 and catalytic oxidation coating 17, lifts subsequent reactions efficiency.Gas enters foul smell adsorption reaction chamber afterwards
12, after switching on power, the electrion of multigroup reaction polar plate 14 in foul smell adsorption reaction chamber 12 produces ozone molecule, hydroxyl free
Produced in the oxidizing species such as base, oxygen radical and high energy electron, gas the macromolecular of stench in above-mentioned Strong oxdiative material and
Small molecule is decomposed under the compound action of ultraviolet, while decomposing the small molecule produced touches the surrounding of foul smell adsorption reaction chamber 12
The catalytic oxidation coating 17 of inwall coating, under the catalysis oxidation of coating, obtains carbon dioxide, nitrogen oxides, sulphur oxidation
The inorganic molecules such as thing water.Bacterium, harmful microorganism present in gas are also in Strong oxdiative material and the compound work of ultraviolet simultaneously
It is killed under;The gas of final purification is excluded into air by foul smell ventilating layer 13, has effectively purified air;By this
The waste gas of reactor for treatment, foul gas reaches more than 99% except rate, and harmful microorganism, the clearance of bacterium reach 99.5%,
The clearance of dust granules reaches 97.8%.
Foul smell ventilating layer 13 includes being located at the vent passages 18 in housing 10 with certain knuckle;The vent passages 18 are by extremely
Few two pieces of identicals ventilation wallboard 19 is formed by connecting;The lower end of vent passages 18 is connected with the reinforcement for fixed ventilation wallboard 19
20.Cause air exhauster 23 in the process of running using vent passages 18, effectively the interference of reduction noise.
Ventilation wallboard 19 be fixedly connected by the first linkage section 19-1, the second linkage section 19-2 and the 3rd linkage section 19-3 and
Into being integrally formed;First linkage section 19-1 is vertical with the top of housing 10 to be connected, and the 3rd linkage section 19-3 is vertical with reinforcement 20
Connection, the second linkage section 19-2 is oblique, for connecting the first linkage section 19-1 and the 3rd linkage section 19-3;Using above-mentioned side
Case so that in operation, the wind direction absorbed is run air exhauster 23 from the bottom to top, what the 3rd adjacent linkage section 19-3 was formed
Vent passages 18 are vertical direction, on wind direction in motion process, due to the settings of the second linkage section 19-2 obliquely, vertically
The wind moved upwards can touch the second linkage section 19-2, produce wind direction skew, give the delay effect of wind direction necessarily, while so that
Wind speed is reduced, and then reduces the brought noise of blower fan motion.
Highly optimized for the ease of the foul smell ventilating layer 13 so that the structure of odor treating device is more convenient and utilizes
Rate is high, the second linkage section 19-2 and the 3rd linkage section 19-3 equal length;First linkage section 19-1 length is the 3rd connection
The 1/2 of section 19-3 length;While reduction noise is ensured, and it can make it that ventilation efficiency is higher.
Second linkage section 19-2 and the first linkage section 19-1 and the 3rd linkage section 19-3 is tilted in 30 °~60 ° of angle, this
Second linkage section 13-2 of device is 45 ° of inclinations, and the effect for reducing noise is more preferable.
The top of housing 10 is provided with discharge duct 21, and the lower end of discharge duct 21 is provided with trumpet type suction opeing 22, trumpet type
The upper end of suction opeing 10 is provided with air exhauster 23;The exhaust outlet of blast pipe 9 is corresponding with the position of aeration-cooling device 7.
Agitating device 6, including main shaft 61, agitating shaft 62 and some stirring vane mechanisms 63 for being socketed on agitating shaft 62;
The outer end of main shaft 61 is fixedly connected with driving gear, and driving gear is driven by motor to be rotated, and then drives 62 turns of main shaft 61 and agitating shaft
Dynamic, agitating shaft 62 is socketed on main shaft 61, and the stirring vane mechanism 63 includes connecting tube 63-1, blade fix bar 63-2 and leaf
Piece 63-3;One end of the blade fix bar 63-2 is fixedly connected with connecting tube 63-1, and the blade fix bar 63-2 other end is used
In fixed blade 63-3;Some connecting tube 63-1 are equidistantly socketed on agitating shaft 62, and adjacent blades fix bar 63-2 is along agitating shaft
62 circumferencial directions have identical angle of inclination;Gap is left between the blade 63-3 of the leftmost side and the exhaust outlet of blast pipe 9, and
Blast pipe 9 is located at blade 63-3 upper end, it is to avoid blade 63-3 blocks the import of blast pipe 9 so that foul smell discharge efficiency is reduced,
With the rotation of agitating shaft 62, drive blade 63-3 to decompose the organic waste decomposed in cabin, stir, improve rubbish
Stirring efficiency.
Blade 63-3 and blade fix bar 63-2 vertical runs, the angle of inclination between blade 63-3 and agitating shaft 62 is
30 °,
Such a design is except the separation for being conducive to organic waste, while being more beneficial for stirring vane 63-3 installation so that in stirring
Blade 63-3 in processing sends out harmonious rise thermally-inhibited, improves the decomposition efficiency for decomposing garbage decomposition thing in cabin;Meanwhile,
Angle of inclination between blade 63-3 and agitating shaft 62 is 45 ° so that whole organic waste produces axially fortune in whipping process
It is dynamic, therefore organic waste stirring can be more abundant, stirring efficiency can be higher.
Blade 63-3 both sides are formed with sharp blade, and sharp blade enables to organic waste to be cut off and smashed,
Decomposition efficiency is improved, blade is laid in the positive and negative of blade 63-3 both sides, enough meet blade 63-3 and rotate feelings in positive and negative alternate
To the stirring of organic waste under condition, so that application is wider.
Connecting tube 63-1 is detachably socketed on agitating shaft 62, is convenient for changing new stirring vane mechanism 63, is blade 63-
3 maintenance work brings facility;Connecting tube 63-1 is corresponding provided with symmetrical two positioning holes 63-1-1,
Agitating shaft 62 is provided with the locating slot being adapted with positioning hole 63-1-1, and positioning hole 63-1-1 is bolted with locating slot.
Connecting tube 63-1 and blade fix bar 63-2 connection goes out to be installed with supporting plate 63-4, and supporting plate 63-4 is symmetrically laid
In connecting tube 63-1 both sides, and supporting plate 63-4 is located at two positioning hole 63-1-1 centre positions;By setting supporting plate 63-4,
The bulk strength of stirring vane mechanism 63 is further increased, stirring efficiency is improved, meanwhile, supporting plate 63-4 length is company
The 1/3 of adapter 63-1 length, and supporting plate 63-4 width successively decreases successively from the bottom to top;It can relax in connecting tube 63-1 and leaf
The friction that the processed rubbish being stirred between piece fix bar 63-2 is produced, can suppress heating relatively low;So, at this
In stirring vane mechanism 63, the heating produced in blade fix bar 63-2, blade 63-3 and decomposition cabin can integrally be suppressed
Obtain smaller;Therefore, supporting plate 63-4 width successively decreases successively from the bottom to top, so the bottom in blade fix bar 63-2, energy
It is enough to implement necessary stir process to being required processing rubbish.
Blade 63-3 in left and right ends stirring vane mechanism 63 is in " A " shape body, and blade 63-3 includes left bank blade
63-3-1, right bank blade 63-3-2 and connection blade 63-3-3;Left bank blade 63-3-1, right bank blade 63-3-2 and company
Meet blade 63-3-3 to be fixedly connected, be integrally formed;The firmness of two end stirring vane mechanisms 63 is added, stirring is improved
Efficiency, blade fix bar 63-2 top is socketed on left bank blade 63-3-1, right bank blade 63-3-2 and connection blade
Between 63-3-3;The direction of the left bank blade 63-3-1 and right bank blade 63-3-2 junction points to agitating shaft 62
Centre position;In the blade 63-3 of " A " shape body, the direction of rotation under the drive of agitating shaft 62 is relative at two ends, and organic waste material exists
Decompose to drive by other blades 63-3 in cabin and stir, when rubbish is pushed to left bank blade to the left and right by intermediate blade 63-3
During 63-3-1 and right bank blade 63-3-2 junction, due to left bank blade 63-3-1 and right bank blade 63-3-2 company
The direction at the place of connecing is directed to the centre position of agitating shaft 62, forms an inside centrifugal force, in left bank blade 63-3-1
With right bank blade 63-3-2 under the drive of agitating shaft 62 so that rubbish material collects to centre, pass through intermediate blade 63-3
Stirring is driven, can carry out realizing that organic waste is decomposing the stirring of cabin interior circulation successively, certainly in whipping process, we can be with
Microwave applicator is set decomposing in cabin, microwave heating is carried out to organic waste by microwave applicator, it is quick to organic materials
Sterilization and fermentation;The blade 63-3 in " A " shape body being oppositely arranged is set so that organic waste is being decomposed in cabin from two ends in
Between move, improve stirring efficiency, meanwhile, it also avoid rubbish decompose cabin two sides accumulation, dead angle can be removed, to prevent
Organic waste plug cannot be sufficiently stirred for and rub at dead angle, it is ensured that use safety.
Blade fix bar 63-2 is provided with 6 or 8, and blade fix bar 63-2 is evenly distributed on agitating shaft 62 vertically
On, the angle of inclination Φ between adjacent blades fix bar 63-2 is identical;The blade fix bar 63-2 of the present embodiment is provided with 8,
Angle of inclination between adjacent blades fix bar 63-2 is 135 °, identical angle of inclination so that the stirring equilibrium degree phase of rubbish
Together, the garbage disposal ability enhancing after decomposition.
The distance between adjacent blades fix bar 63-2 is less than blade 63-3 length, and blade 63-3 length is solid for blade
The 1/2 of fixed pole 63-2 length;Blade fix bar 63-2 a diameter of connecting tube 63-1 length 1/2.
Through hole 63-3-4 is laid with blade 63-3, through hole 63-3-4 is provided with two, is symmetrically laid in blade fix bar
63-2 both sides;The through hole 63-3-4 is trough type manhole, and through hole 63-3-4 length is the 1/5 of blade 63-3 length,
Through hole 63-3-4 width is the 1/2 of blade 63-3 width;Through hole 63-3-4 is laid with blade 63-3, through hole 63-3-4 energy
Blade 63-3 load is enough effectively reduced, while molecule in rubbish can also be made to be stirred point by through hole 63-3-4
From, and mixing speed is fast, and stirring efficiency is high.
The foregoing description of the disclosed embodiments, enables professional and technical personnel in the field to realize or using the present invention.
A variety of modifications to these embodiments will be apparent for those skilled in the art, as defined herein
General Principle can be realized in other embodiments without departing from the spirit or scope of the present invention;Therefore, it is of the invention
The embodiments shown herein is not intended to be limited to, and is to fit to and principles disclosed herein and features of novelty phase one
The most wide scope caused.
Although more having used reference in figure herein:Processor body 1, sort operation platform 2, material pour spout 3,
Pulverizer 4, stir storehouse 5, agitating device 6, main shaft 61, agitating shaft 62, stirring vane mechanism 63, connecting tube 63-1, positioning hole 63-
1-1, blade fix bar 63-2, blade 63-3, left bank blade 63-3-1, right bank blade 63-3-2, connect blade 63-3-3,
Through hole 63-3-4, supporting plate 63-4, aeration-cooling device 7, rubbish deodorization purifier 8, blast pipe 9, housing 10, rubbish filtering
Layer 11, foul smell adsorption reaction chamber 12, foul smell ventilating layer 13, reaction polar plate 14, ultraviolet mercury lamp 15, power supply 16, catalytic oxidation
Coating 17, vent passages 18, wallboard 19 of divulging information, the first linkage section 19-1, the second linkage section 19-2, the 3rd linkage section 19-3, plus
Strengthening tendons 20, discharge duct 21, trumpet type suction opeing 22, the grade term of air exhauster 23, but it is not precluded from the possibility using other terms
Property;It is used for the purpose of more easily describing and explaining the essence of the present invention using these terms;It is construed as any one
Additional limitation is all disagreed with spirit of the present invention.
Claims (10)
1. the odor removal of organic waste microbial processor, it is characterised in that:Including processor body(1);The processor
Body(1)It is provided with sort operation platform(2);The sort operation platform(2)On be provided with material pour spout(3);Processor body
(1)It is interior to be provided with stir storehouse(5)And pulverizer(4), stir storehouse(5)Charging aperture and sort operation platform(2)Material pour spout(3)
Position is corresponding;Pulverizer(4)Positioned at material pour spout(3)Bottom and stir storehouse(5)Charging aperture between;Stir storehouse(5)Top
Portion is provided with aeration-cooling device(7), stir storehouse(5)Inside it is laid with agitating device(6);Stir storehouse(5)Side wall is connected with exhaust
Pipe(9), blast pipe(9)On be connected with rubbish deodorization purifier(8), rubbish deodorization purifier(8)It is fixedly arranged on processor sheet
Body(1)On.
2. the odor removal of organic waste microbial processor according to claim 1, it is characterised in that:The rubbish is removed
Smelly purifier(8)Including housing(10), positioned at housing(10)The rubbish filtering layer inside laid successively from the bottom to top(11), foul smell
Adsorption reaction chamber(12)With foul smell ventilating layer(13);The housing(7)It is made of stainless steel;Rubbish filtering layer(11), foul smell inhale
Reaction enclosure chamber(12)With foul smell ventilating layer(13)Between be respectively kept with gap;The rubbish filtering layer(11)Filtered for activated carbon
Activated carbon is filled with layer, activated carbon filter layer;The foul smell adsorption reaction chamber(12)Inside be arranged in parallel multigroup reaction polar plate
(14), foul smell adsorption reaction chamber(12)Multiple ultraviolet mercury lamps are uniformly installed on surrounding inwall(15), reaction polar plate(14)With it is ultraviolet
Mercury lamp(15)Respectively with housing(10)Outside power supply(16)It is connected, and surrounding inwall coating catalytic oxidation coating
(17).
3. the odor removal of organic waste microbial processor according to claim 2, it is characterised in that:The foul smell leads to
Stratification of wind(13)Including positioned at housing(10)The interior vent passages with certain knuckle(18);The vent passages(18)By at least two pieces
Identical ventilation wallboard(19)It is formed by connecting;Vent passages(18)Lower end is connected with for fixed ventilation wallboard(19)Reinforcement
(20).
4. the odor removal of organic waste microbial processor according to claim 3, it is characterised in that:The ventilated walls
Plate(19)By the first linkage section(19-1), the second linkage section(19-2)With the 3rd linkage section(19-3)It is formed by fixedly connecting, one
Shaping;First linkage section(19-1)With housing(10)Top vertically connect, the 3rd linkage section(19-3)With reinforcement(20)Hang down
It is direct-connected to connect, the second linkage section(19-2)Obliquely, for connecting the first linkage section(19-1)With the 3rd linkage section(19-3);Institute
State the second linkage section(19-2)With the 3rd linkage section(19-3)Equal length;First linkage section(19-1)Length for the 3rd connect
Connect section(19-3)The 1/2 of length;Second linkage section(19-2)With the first linkage section(19-1)With the 3rd linkage section(19-3)
Tilted in 30 °~60 ° of angles.
5. the odor removal of organic waste microbial processor according to claim 3, it is characterised in that:The housing
(10)Top is provided with discharge duct(21), discharge duct(21)Lower end is provided with trumpet type suction opeing(22), trumpet type exhausting
Mouthful(10)Upper end is provided with air exhauster(23).
6. the odor removal of organic waste microbial processor according to claim 1, it is characterised in that:The blast pipe
(9)Exhaust outlet and aeration-cooling device(7)Position it is corresponding.
7. the odor removal of organic waste microbial processor according to claim 1, it is characterised in that:The stirring dress
Put(6)
Including main shaft(61), agitating shaft(62)Be socketed on agitating shaft(62)On some stirring vane mechanisms(63);Agitating shaft
(62)It is socketed on main shaft(61)On, the stirring vane mechanism(63)Including connecting tube(63-1), blade fix bar(63-2)With
Blade(63-3);The blade fix bar(63-2)One end and connecting tube(63-1)It is fixedly connected, blade fix bar(63-2)
The other end be used for fix blade(63-3);Some connecting tubes(63-1)Equidistantly it is socketed on agitating shaft(62)On, adjacent blades are solid
Fixed pole(63-2)Along agitating shaft(62)Circumferencial direction has identical angle of inclination;The blade of the leftmost side(63-3)With blast pipe
(9)Exhaust outlet between leave gap, and blast pipe(9)Positioned at blade(63-3)Upper end.
8. the odor removal of organic waste microbial processor according to claim 7, it is characterised in that:The blade
(63-3)With blade fix bar(63-2)Vertical runs, blade(63-3)With agitating shaft(62)Between angle of inclination for 30 °~
45°。
9. the agitating device of organic waste microbial processor according to claim 1, it is characterised in that:The connecting tube
(63-1)Detachably it is socketed on agitating shaft(62)On, connecting tube(63-1)It is provided with two symmetrical positioning holes(63-1-1),
Corresponding, agitating shaft(62)It is provided with and positioning hole(63-1-1)The locating slot being adapted, positioning hole(63-1-1)With
Locating slot is bolted.
10. the odor removal of organic waste microbial processor according to claim 3, it is characterised in that:The connection
Pipe(63-1)With blade fix bar(63-2)Connection go out to be installed with supporting plate(63-4), supporting plate(63-4)The symmetrical company of being laid in
Adapter(63-1)Both sides, and supporting plate(63-4)Positioned at two positioning holes(63-1-1)Centre position.
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CN110563209A (en) * | 2019-10-10 | 2019-12-13 | 深圳市驭智装备技术有限公司 | Deodorization mechanism of reaction kettle |
CN112170449A (en) * | 2020-09-15 | 2021-01-05 | 北京德鑫合众环保工程有限公司 | Kitchen waste treatment equipment capable of deodorizing by using waste heat |
CN113767188A (en) * | 2019-04-24 | 2021-12-07 | 应用材料公司 | Reactor for coating particles in a stationary chamber with rotating paddles |
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Application publication date: 20170801 |