CN106269792B - A kind of refuse disposal system and waste disposal method - Google Patents
A kind of refuse disposal system and waste disposal method Download PDFInfo
- Publication number
- CN106269792B CN106269792B CN201610707064.4A CN201610707064A CN106269792B CN 106269792 B CN106269792 B CN 106269792B CN 201610707064 A CN201610707064 A CN 201610707064A CN 106269792 B CN106269792 B CN 106269792B
- Authority
- CN
- China
- Prior art keywords
- unit
- rubbish
- airtight
- solid content
- gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 238000000034 method Methods 0.000 title claims abstract description 20
- 239000002699 waste material Substances 0.000 title claims abstract description 14
- 239000010813 municipal solid waste Substances 0.000 claims abstract description 184
- 239000007789 gas Substances 0.000 claims abstract description 84
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 72
- 239000007787 solid Substances 0.000 claims abstract description 66
- 238000012545 processing Methods 0.000 claims abstract description 61
- 239000010865 sewage Substances 0.000 claims abstract description 48
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 36
- 239000004519 grease Substances 0.000 claims abstract description 33
- 238000001035 drying Methods 0.000 claims abstract description 32
- 238000002485 combustion reaction Methods 0.000 claims abstract description 31
- 230000001376 precipitating effect Effects 0.000 claims abstract description 31
- 238000001354 calcination Methods 0.000 claims abstract description 28
- 230000006835 compression Effects 0.000 claims abstract description 20
- 238000007906 compression Methods 0.000 claims abstract description 20
- 239000010802 sludge Substances 0.000 claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 55
- 239000002893 slag Substances 0.000 claims description 18
- 239000004566 building material Substances 0.000 claims description 15
- 241001465754 Metazoa Species 0.000 claims description 13
- 238000005238 degreasing Methods 0.000 claims description 13
- 238000005273 aeration Methods 0.000 claims description 12
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 11
- 230000001580 bacterial effect Effects 0.000 claims description 11
- 239000001301 oxygen Substances 0.000 claims description 11
- 229910052760 oxygen Inorganic materials 0.000 claims description 11
- 239000002994 raw material Substances 0.000 claims description 10
- 239000002002 slurry Substances 0.000 claims description 7
- 239000007921 spray Substances 0.000 claims description 7
- 238000004140 cleaning Methods 0.000 claims description 6
- 238000004148 unit process Methods 0.000 claims 1
- 238000000926 separation method Methods 0.000 abstract description 12
- 238000005276 aerator Methods 0.000 abstract description 8
- 239000000047 product Substances 0.000 description 21
- 239000000463 material Substances 0.000 description 13
- 210000004027 cell Anatomy 0.000 description 12
- 238000000465 moulding Methods 0.000 description 10
- 229910001872 inorganic gas Inorganic materials 0.000 description 8
- 241000894006 Bacteria Species 0.000 description 7
- 238000001125 extrusion Methods 0.000 description 6
- 230000005484 gravity Effects 0.000 description 6
- 238000001514 detection method Methods 0.000 description 5
- 238000010248 power generation Methods 0.000 description 4
- -1 silt Substances 0.000 description 4
- 229910001220 stainless steel Inorganic materials 0.000 description 4
- 239000010935 stainless steel Substances 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- 230000007613 environmental effect Effects 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- 239000003337 fertilizer Substances 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000000919 ceramic Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 239000004744 fabric Substances 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 239000012634 fragment Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 2
- 239000010985 leather Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 239000011368 organic material Substances 0.000 description 2
- 210000004681 ovum Anatomy 0.000 description 2
- 239000000123 paper Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 230000003760 hair shine Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 230000001473 noxious effect Effects 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000011112 process operation Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000010801 sewage sludge Substances 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000002341 toxic gas Substances 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
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
-
- 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B2101/00—Type of solid waste
- B09B2101/02—Gases or liquids enclosed in discarded articles, e.g. aerosol cans or cooling systems of refrigerators
Landscapes
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Processing Of Solid Wastes (AREA)
- Treatment Of Sludge (AREA)
Abstract
The present invention provides a kind of refuse disposal system and waste disposal method, which includes garbage collection unit；The airtight rubbish unit connecting with the garbage inlet of garbage collection unit is equipped with nitrogen aerator in airtight rubbish unit, for garbage disposal to be obtained gas, sewage, solid content and mud；The air processing unit connecting with the gas vent of airtight rubbish unit, air processing unit carry out gas compression separation；With the mud press-forming units of the solid content outlet connection of airtight rubbish unit；The precipitating oil removal unit being connect with the outlet of sewer of airtight rubbish unit；The solid content drying unit being connect with the sludge outlet of airtight rubbish unit；The biochemical treatment unit being connect with precipitating oil removal unit by pipeline；The combustion chamber that the outlet of outlet, air processing unit with solid content drying unit and the grease outlets for precipitating oil removal unit are separately connected；With the calcining compartment of the outlet connection of solid content press-forming units.The system can realize rubbish innoxious.
Description
Technical field
The present invention relates to technical field of waste treatment more particularly to a kind of refuse disposal systems and waste disposal method.
Background technique
City is a main feature of human civilization, and a large amount of people concentrates in together, and is generated in life and work a large amount of
Waste forms Urban Environmental Problem, and has the tendency that increasing year by year.According to statistics, every 1,000,000 permanent resident population city, day
The quantity of refuse (dry weight, the same below) generated is about 300 tons, only Chinese, just up to 180,000 ton per days, it is global then be up to 900,000 tons/
Day, process demand is very huge.
Currently, most domestic incineration firing treatment plant mainly uses at refuelling the loss of ignition method and room temperature classification
Reason.The ignition temperature of refuelling the loss of ignition method is usually no more than 800 DEG C, and 400 DEG C of combustion zone local temperature is hereinafter, can not have
Effect burning, and a large amount of toxic gas dioxin is brought to generate, bring huge environment side effect；Since burning is not thorough, mostly
In number situation, rubbish can only be reduced within 30%, and there is still a need for landfills for other parts.After the classification of room temperature classification, part can rot
Organic matter, be used to fermentation process, or add bacterium processing, form bio-fertilizer；Remaining is unserviceable, after being reduced, send landfill
Field processing；The consequence of room temperature classification processing is that the harmful substance in bacterium does not add processing, and as fertilizer flows, is formed new
Environment hidden danger；Fertilizer cannot be made, and the part of other use can not be done, will also continue to fill.
The method of above-mentioned garbage disposal does not solve garbage problem really, it would therefore be highly desirable to need to develop at a kind of rubbish
Reason mode realizes the innoxious of rubbish, will really solve the problem of rubbish.
Summary of the invention
In view of this, the purpose of the present invention is to provide a kind of refuse disposal system and waste disposal method, the present invention is mentioned
Treated that rubbish can be realized is innoxious for the refuse disposal system of confession, and the residue without any need landfill.
The present invention provides a kind of refuse disposal systems, including garbage collection unit；
The airtight rubbish unit connecting with the garbage inlet of the garbage collection unit is equipped in the airtight rubbish unit
Nitrogen aerator, for garbage disposal to be obtained gas, sewage, solid content and mud；
The air processing unit connecting with the gas vent of the airtight rubbish unit, the air processing unit carry out gas
The compression of body separates；
The mud press-forming units being connect with the sludge outlet of the airtight rubbish unit；
The precipitating oil removal unit being connect with the outlet of sewer of the airtight rubbish unit；
With the solid content drying unit of the solid content outlet connection of the airtight rubbish unit；
The biochemical treatment unit being connect with the precipitating oil removal unit by pipeline；
The outlet of outlet, air processing unit with the solid content drying unit and the grease outlets for precipitating oil removal unit
The combustion chamber being separately connected；
With the calcining compartment of the outlet connection of the mud press-forming units.
Preferably, the refuse disposal system further includes fishing slag slag conveyer；The fishing slag slag conveyer is arranged in airtight rubbish
The solid content exit of unit.
Preferably, the refuse disposal system further includes scraper plate slurry conveying machine；The scraper plate slurry conveying machine is arranged in airtight rubbish
At the sludge outlet of rubbish unit.
Preferably, the refuse disposal system further includes the sewage connecting with the sewage inlet of the airtight rubbish unit
Pond.
The present invention provides a kind of waste disposal methods, comprising the following steps:
The rubbish that garbage collection unit is collected is transported to airtight rubbish unit, by nitrogen Air Exposure, obtain gas,
Sewage, solid content and mud；
It delivers the gas to air processing unit to be handled, obtains organic gas；Solid content is transported to solid
The processing of object press-forming units；By sewage transport to precipitating oil removal cell processing, the sewage and grease except degreasing are respectively obtained,
The sewage except degreasing is passed through into biochemical treatment unit, obtains middle water；By mud be transported to mud press-forming units into
Row processing；
Product, organic gas and grease that the solid content drying unit is handled are delivered to combustion chamber to fire
It burns；
The product that mud press-forming units are handled is delivered to calcining compartment to calcine, obtains can be used as building materials original
The calcined product of material.
Preferably, the temperature that nitrogen is aerated in the airtight rubbish unit is 0 DEG C~40 DEG C；The time of nitrogen aeration is big
In equal to 4 hours；The pressure of nitrogen aeration is more than or equal to 0.4MPa.
Preferably, the air processing unit is by the way of compression separation；
The isolated pressure of the compression is 0.5~1.4MPa.
Preferably, the temperature of the biochemical treatment cell processing is 0 DEG C~50 DEG C；The biochemical treatment cell processing when
Between be for 24 hours~72h.
Preferably, the burning is more than or equal to 99% oxygen using mass fraction；The temperature of the burning is 1200 DEG C
~2000 DEG C.
Preferably, the temperature of the calcining is 400 DEG C~1000 DEG C.
The present invention provides a kind of refuse disposal systems, including garbage collection unit；With the rubbish of the garbage collection unit
The airtight rubbish unit of rubbish entrance connection, nitrogen aerator is equipped in the airtight rubbish unit, for obtaining garbage disposal
To gas, sewage, solid content and mud；The air processing unit being connect with the gas vent of the airtight rubbish unit, it is described
Air processing unit carries out the compression separation of gas；The mud extrusion forming being connect with the sludge outlet of the airtight rubbish unit
Unit；The precipitating oil removal unit being connect with the outlet of sewer of the airtight rubbish unit；With the solid of the airtight rubbish unit
The solid content drying unit of object outlet connection；The biochemical treatment unit being connect with the precipitating oil removal unit by pipeline；With institute
It states the outlet of solid content drying unit, the outlet of air processing unit and precipitates the combustion that the grease outlets of oil removal unit are separately connected
Burn room；With the calcining compartment of the outlet connection of the mud press-forming units.Refuse disposal system provided by the invention can incite somebody to action
Rubbish realizes residue that is innoxious, and filling without any need.
Detailed description of the invention
Fig. 1 is the flow diagram that refuse disposal system provided by the invention handles rubbish.
Specific embodiment
The present invention provides a kind of refuse disposal systems, including garbage collection unit；
The airtight rubbish unit connecting with the garbage inlet of the garbage collection unit is equipped in the airtight rubbish unit
Nitrogen aerator, for garbage disposal to be obtained gas, sewage, solid content and mud；
The air processing unit connecting with the gas vent of the airtight rubbish unit, the air processing unit carry out gas
The compression of body separates；
The mud press-forming units being connect with the sludge outlet of the airtight rubbish unit；
The precipitating oil removal unit being connect with the outlet of sewer of the airtight rubbish unit；
With the solid content drying unit of the solid content outlet connection of the airtight rubbish unit；
The biochemical treatment unit being connect with the precipitating oil removal unit by pipeline；
The outlet of outlet, air processing unit with the solid content drying unit and the grease outlets for precipitating oil removal unit
The combustion chamber being separately connected；
With the calcining compartment of the outlet connection of the mud press-forming units.
Refuse disposal system provided by the invention includes garbage collection unit.In the present invention, the garbage collection unit
For collecting pit, in a specific embodiment of the present invention, the shape of the collecting pit is cylindrical body, overall diameter
Interior diameterAerial part height 6m, under ground portion height 2m；The liner material of collecting pit is stainless steel.?
In the present invention, the garbage collection unit is connect by garbage shaft with following airtight garbage pools.Present invention preferably employs water flows
Rubbish is sent in garbage shaft by mode.It is rolled in garbage shaft and dividing processing.In the present invention, the rubbish
Multiple protective devices are set up in channel, in case personnel and article fall.
Refuse disposal system provided by the invention includes the airtight rubbish connecting with the garbage inlet of the garbage collection unit
Rubbish unit is equipped with nitrogen aerator in the airtight rubbish unit, for garbage disposal to be obtained gas, sewage, solid content
And mud.In the present invention, the airtight rubbish unit includes airtight garbage pool, cleaning spray thrower and gas-tight door.In the present invention
Specific embodiment in, the specification of the airtight garbage pool is 60m × 60m × 3m, and dischargeable capacity is about 5000m3.In the present invention
In, the airtight garbage pool is provided with feeding inlet, for the input of rubbish.In the present invention, the top of the airtight garbage pool
Equipped with cleaning spray thrower；The top of airtight garbage pool is arranged in the cleaning spray thrower, so that rubbish is cooled down by spray；It is described clear
The water that washing and spraying device uses is preferably middle water described in following technical proposals.In the present invention, rubbish enters airtight rubbish
Chi Zhonghou is closed feeding inlet using gas-tight door；When process operation, the gas-tight door is in close state；The gas-tight door is also
For setting air valve and pipeline.In a specific embodiment of the present invention, the gas-tight door is preferably provided with 6 sets.After aeration,
The present invention starts cleaning spray thrower and cleans the top of airtight garbage pool everywhere；Present invention preferably employs water to clean airtight garbage pool
Top is everywhere.
After rubbish enters airtight rubbish unit, start nitrogen aerator；The present invention kills gas by being passed through excessive nitrogen
All worm's ovums, toy, microorganism and part bacterium in close garbage pool.Bottom is equipped with blender in airtight garbage pool；Aeration
After, start the blender, so that specific gravity is greater than the article of water, such as silt, glass, metal, ceramics in rubbish, it is heavy
Drop to bottom of pond；So that perishable organic matter, such as dish leaf, food, animal fragment etc. are dissolved in the water, obtain sewage；So that rubbish
In article having a specific gravity smaller than that of water, such as paper, plastics, chemical fibre, cloth, timber, leather are bubbled through the water column.
Refuse disposal system provided by the invention includes at the gas for the gas vent connection connecting with airtight rubbish unit
Unit is managed, the air processing unit carries out the compression separation of gas.When charged pressure be no less than 0.4MPa pressure 99.9% with
The nitrogen of upper concentration starts gas concentration unit.In the present invention, the gas concentration unit is membrane separation device；The film
Separator includes air compressor machine, and gas is separated by the compression of air compressor machine, realizes the recycling of gas；Pressure when the compression separation
Power is preferably 0.5~1.4MPa.Organic gas in gas is collected by compression to be stored to air collector, then passes through Pipeline transport extremely
It burns in combustion chamber；The organic gas includes overflowing all kinds of carbon containing organic gas from airtight garbage pool；In the gas
Nitrogen and other inorganic gas discharged after detection is qualified；The nitrogen and other inorganic gas meet national discharge through detection
It is discharged after standard GB14554-93 " emission standard for odor pollutants " is qualified.
Refuse disposal system provided by the invention includes that the mud connecting with the sludge outlet of the airtight rubbish unit squeezes
Molded unit.In the present invention, it is also preferable to include scraper plate slurry conveying machines, the scraper plate slurry conveying machine to set for the refuse disposal system
At the sludge outlet for setting airtight rubbish unit.In the present invention, the mud press-forming units include dry pond, airtight rubbish
The outlet of unit is connect with the entrance in dry pond.In the present invention, specific gravity in rubbish is greater than the object of water by the scraper plate slurry conveying machine
Product, i.e., the bottom sediment that can be picked up in garbage pool are collected into dry pond；It is extracted with sludge pump to dry the part that cannot be picked up
Dry pond.The present invention preferably crushes the product of the mud press-forming units with screw mill, after being cleaned with clear water, shines
Dry, drying is spare.The present invention mixes obtained drying sediment and binding material, with shaping mechanism at building materials, send to warehouse
It is spare.The building materials are delivered to calcining compartment again and are calcined.
Refuse disposal system provided by the invention include the precipitating that is connect with the outlet of sewer of the airtight rubbish unit every
Oily unit.In the present invention, the sewage transport that the airtight rubbish cell processing obtains extremely precipitating oil removal unit.In the precipitating
The grease generated in oil removal unit is by oil rig, and by water-oil separating, grease therein is delivered to spare in grease pond.This hair
It is bright the grease in grease pond is preferably transported to combustion chamber described in following technical proposals to go to burn.
Refuse disposal system provided by the invention includes the biochemical treatment unit being connect with precipitating oil removal unit by pipeline.
The present invention is by the sewage transport after precipitating oil removal cell processing to biochemical treatment unit.
In the present invention, the biochemical treatment unit includes bacterial treatment unit and aquatic animals and plants processing unit, described
The entrance of bacterial treatment unit is connect with the outlet of precipitating oil removal unit, the outlet of the bacterial treatment unit and aquatic animals and plants
The entrance of processing unit connects.Bacterium is added in the bacterial treatment unit, removes metal ion and noxious material therein,
Obtain eutrophy sewage.After obtaining eutrophic water, the present invention is continued with using aquatic animals and plants, by multi-absorption, makes water
Middle indices are sent into the middle pond with the outlet connection of aquatic animals and plants processing unit, middle water close to city's originally water quality standard
The water in pond is input to cleaning spray thrower, garbage shaft and other desired occasion by water pump.If there still have in middle pond to be extra
Water is delivered to artificial Swampy Areas, for producing water plant and animal.
Refuse disposal system provided by the invention includes the solid with the solid content of airtight rubbish unit outlet connection
Object dries pond.
In the present invention, it is also preferable to include fishing slag slag conveyers, the fishing slag slag conveyer setting to exist for the refuse disposal system
The solid content exit of airtight rubbish unit.In the present invention, the fishing slag slag conveyer will float in water and waterborne in garbage pool
Solid content collect to specified cold sink, after washing with water, solid is sent by the entrances of solid content press-forming units
In object press-forming units.It is equipped with squeezing machine in the press-forming units, squeezes out contained humidity in solid content, extracts moisture
Rubbish afterwards, which is sent to drying room, dries, and after drying, then is crushed with pulverizer, is sent into Bunker and stacks spare, then is delivered to burning
It burns room.
Refuse disposal system provided by the invention further includes and the solid content dries the outlet in pond, air processing unit
Export the combustion chamber connected with the grease outlets of precipitating oil removal unit.In the present invention, the solid content in above-mentioned technical proposal, oil
The organic gas that the grease and air processing unit collected in rouge pond are collected into is transported to combustion chamber and carries out burning processing.This hair
It is bright to be lighted by the way of electronic striking.In the combustion chamber, the gas used that burns is high-concentration oxygen for concentration,
Preferably mass concentration is more than or equal to 99% oxygen；The temperature of the burning is preferably 1200 DEG C~2000 DEG C.
Refuse disposal system provided by the invention further includes the calcining compartment with the outlet connection of solid content press-forming units.
In the present invention, the solid content after the solid content extrusion process cell processing is delivered to calcining compartment and is calcined.Calcining compartment produces
Raw heat can be used to do the energy dried.The calcined product that calcining compartment generates may be used as the production raw material of building materials.
It is also preferable to include connect with the sewage inlet of the airtight rubbish unit refuse disposal system provided by the invention
Cesspool.In the present invention, the water in the cesspool is preferred from municipal sewage net；Sewage in the cesspool preferably and
Rubbish enters in airtight rubbish unit the processing for carrying out rubbish together.
The present invention provides a kind of waste disposal methods, comprising the following steps:
The rubbish that garbage collection unit is collected is transported to airtight rubbish unit, by nitrogen Air Exposure, obtain gas,
Sewage, solid content and mud；
It delivers the gas to air processing unit to be handled, obtains organic gas；Solid content is transported to solid
The processing of object drying unit；By sewage transport to precipitating oil removal cell processing, the sewage and grease except degreasing are respectively obtained, by institute
The sewage except degreasing is stated by biochemical treatment unit, obtains middle water；Mud is transported at mud press-forming units
Reason；
Product, organic gas and grease that the solid content drying unit obtains are delivered to combustion chamber to burn；
The product that the mud press-forming units are handled is delivered to calcining compartment to calcine, can be used as
The calcined product of building materials raw material.
The rubbish that garbage collection unit is collected is transported to airtight rubbish unit and is obtained by nitrogen Air Exposure by the present invention
To gas, sewage, solid content and mud.In the present invention, the garbage collection unit is collecting pit.In specific reality of the invention
It applies in example, the shape of the collecting pit is cylindrical body, overall diameterInterior diameterAerial part
Height 6m, under ground portion height 2m；The liner material of collecting pit is stainless steel.The present invention kills gas by being passed through excessive nitrogen
All worm's ovums, toy, microorganism and part bacterium in close garbage pool.Bottom is equipped with blender in airtight garbage pool；Aeration
After, start the blender, so that specific gravity is greater than the article of water, such as silt, glass, metal, ceramics in rubbish, it is heavy
Drop to bottom of pond；So that perishable organic matter, such as dish leaf, food, animal fragment etc. are dissolved in the water, obtain sewage；So that rubbish
In article having a specific gravity smaller than that of water, such as paper, plastics, chemical fibre, cloth, timber, leather are bubbled through the water column.In the present invention, described
The temperature of nitrogen aeration is preferably 0 DEG C~40 DEG C；The time of nitrogen aeration is preferably greater than to be equal to 4 hours；The pressure of nitrogen aeration
Power is preferably greater than or equal to 0.4MPa.
The present invention delivers the gas to air processing unit and handles, and obtains organic gas.In the present invention, institute
Air processing unit is stated preferably by the way of compression separation；The isolated pressure of the compression is preferably 0.5~1.4MPa.
The mud is transported to the processing of mud press-forming units by the present invention.In the present invention, the mud preferably and
After binding material mixing, then using molding machine well known to those skilled in the art progress extrusion forming.In the present invention, described viscous
Tying material includes one of all kinds of raw materials of brickmaking, mixed mud or a variety of；The mass ratio of the mud and binding material is adjustable, becomes silted up
The mass ratio of mud and binding material is preferably 1:0.1~2.Obtained extrusions is stored to warehouse, it is spare, then go to forge
Room is burnt to be calcined.
Sewage transport to precipitating oil removal cell processing, is respectively obtained the sewage and grease except degreasing, by institute by the present invention
The sewage except degreasing is stated by biochemical treatment cell processing, obtains middle water.In the present invention, the precipitating oil removal unit is preferred
For sedimentation basin.Present invention preferably employs oil rigs well known to those skilled in the art to separate the oil in sewage with water.This hair
It is bright to pass through biochemical treatment unit except the sewage of degreasing, obtain middle water.In the present invention, the biochemical treatment cell processing is excellent
Choosing includes successively handling by bacterial treatment and aquatic animals and plants；The bacterium used when the bacterial treatment includes fungi and anaerobism
One of bacterium is a variety of；Water flow when aquatic animals and plants processing is preferably low speed；The low speed is preferably 0.1m3/
S~1m3/s；The present invention preferably by except the water biochemical treatment of degreasing is to the 3 above standard of class water of environmental emission, is then drained into
Middle pond.
Mud is transported to dry pond and is dried by the present invention.In the present invention, the temperature of the drying process is
80~400 DEG C；The time of the drying process is 0.5~4h.
After obtaining organic gas and grease, product, organic gas and oil that the present invention obtains the dry pond of the solid content
Rouge is transported to combustion chamber and burns.In the present invention, the burning preferably uses high-concentration oxygen, more preferably using quality point
Number is more than or equal to 99% oxygen；The temperature of the burning is 1200 DEG C~2000 DEG C.In the present invention, the grease and organic
Gas is preferably pumped into combustion chamber according to a certain percentage and burns；Oxygen mistake when the dosage of the oxygen preferably presses completely burned
Amount more than 1%, the dosage of the organic gas be subject to garbage treating pool separate total amount；The dry pond of the solid content obtains
The speed that product is delivered to combustion chamber is preferably 0.5m/s~1.2m/s.In a combustion chamber, it is preferred to use the mode of electronic ignition,
Burn the CO generated2Gas and H2O gas is sprayed through the spout of combustion chamber pushes connected turbo blade, and band movable vane piece rotates,
Driven generator power generation, the high-temperature tail gas after power generation are sent into calcining compartment, the origin of heat as calcining compartment.The present invention preferably will be through
The heat of tail gas is reached drying room, the solid that drying press-forming units squeeze by heat exchanger by the tail gas after crossing calcining compartment
Object.Gas after drying room is discharged through exhaust outlet.
The product that the mud press-forming units are handled is delivered to calcining compartment and calcined by the present invention, and obtaining can
Calcined product as building materials raw material.In the present invention, the temperature of the calcining is preferably 400 DEG C~1000 DEG C.The present invention will
It calcines obtained calcined product and is used as building materials raw material.The raw material of brickmaking can be such as used to or be used as building packing material.
The technique that the present invention is used to brickmaking to calcined product does not have special limitation, and use is well known to those skilled in the art
Brickmaking technology.
Fig. 1 is the flow diagram that refuse disposal system provided by the invention handles rubbish, carries out rubbish using this system
The process of processing are as follows:
The rubbish that collecting pit is collected is transported in airtight garbage pool by garbage shaft, nitrogen is carried out in airtight garbage pool
After gas Air Exposure, by nitrogen Air Exposure, gas, sewage, solid content and mud are obtained；The gas is passed through into compressor
Compression separation is carried out, organic gas and inorganic gas, outlet after inorganic gas detection is qualified are obtained；Organic gas is defeated by pipeline
Combustion chamber is sent to go to burn.Sewage transport is handled into precipitating oil separator, grease is extracted by oil-collecting by oil rig
Then Chi Zhong is pumped to combustion chamber and goes to burn, again except the sewage of degreasing successively passes through biochemical treatment system and aquatic culture zone
It is handled, obtains middle water, stored into middle pond, the middle water can go in airtight garbage pool to be sprayed.Mud is adopted
It is exported, then extrusion forming, is crushed with scraper plate slurry conveying machine, then drying is stored to warehouse, then be delivered to calcining compartment and go to calcine.
Solid content is picked up using fishing slag slag conveyer, extracts, then dries, crush, be stored in warehouse, then be delivered to combustion chamber and go to fire
It burns；It is sent into oxygen simultaneously in combustion chamber, after electronic ignition, generates air-flow, pushes gas-turbine, band movable vane piece rotates, driving hair
Electric power generation；Tail gas after power generation is sent into calcining compartment heating and prepares finished product building materials；Tail gas after calcining compartment passes through heat exchanger
Heat is set to be delivered to drying room, the origin of heat as drying room；Gas after drying room discharges again.
The present invention provides a kind of refuse disposal systems, including garbage collection unit；With the rubbish of the garbage collection unit
The airtight rubbish unit of rubbish entrance connection, nitrogen aerator is equipped in the airtight rubbish unit, for obtaining garbage disposal
To gas, sewage, solid content and mud；The air processing unit being connect with the gas vent of the airtight rubbish unit, it is described
Air processing unit carries out the compression separation of gas；The mud extrusion forming being connect with the sludge outlet of the airtight rubbish unit
Unit；The precipitating oil removal unit being connect with the outlet of sewer of the airtight rubbish unit；With the solid of the airtight rubbish unit
The dry pond of the solid content of object outlet connection；The biochemical treatment unit being connect with the precipitating oil removal unit by pipeline；With it is described
The burning that the grease outlets of the outlet in the dry pond of solid content, the outlet of air processing unit and precipitating oil removal unit are separately connected
Room；With the calcining compartment of the outlet connection of the mud press-forming units.Refuse disposal system provided by the invention can be by rubbish
Rubbish realizes residue that is innoxious, and filling without any need.
In order to further illustrate the present invention, below with reference to embodiment to a kind of refuse disposal system provided by the invention and rubbish
Rubbish processing method is described in detail, but they cannot be interpreted as limiting the scope of the present invention.
Embodiment 1
It is cylindrical body, overall diameter by shapeInterior diameterAerial part height 6m,
Under ground portion height 2m, liner material are transported to rule for 1000 tons of rubbish that the collecting pit of stainless steel is collected by the way of water flow
Lattice are 60m × 60m × 3m, and dischargeable capacity is about 5000m3Airtight garbage pool in, by used at 25 DEG C mass fraction for
99.9% or more nitrogen Air Exposure 5h, pressure when nitrogen is aerated is 0.5MPa, obtains gas, sewage, solid content and silt
Mud；After aeration, the top of airtight garbage pool is cleaned everywhere using following middle water；
When above-mentioned nitrogen charged pressure is not less than 0.4MPa, starts air compressor machine, deliver the gas to gas treatment
In unit, compression separating treatment is carried out using air compressor machine, the pressure for compressing separation is 1.3MPa, obtains organic gas and inorganic gas
Body is collected by compression and is stored to air collector, then burnt by Pipeline transport into combustion chamber；The organic gas includes
All kinds of carbonaceous organic materials overflowed in closed pond；Nitrogen and other inorganic gas in gas meet national emission standard through detection
It is discharged after GB14554-93 " emission standard for odor pollutants " is qualified；
Solid content is transported in specified cold sink using fishing slag slag conveyer, after being cleaned with clear water, is transported to solid content
Press-forming units are handled: it uses squeezing machine to squeeze out to rubbish water content and is dried after 10%~25%, to send to drying room,
It is crushed again with pulverizer after drying, it is spare to be sent into Bunker stacking, then be delivered to combustion chamber and burn；
Sewage transport is handled into grease pond, respectively obtains the sewage and grease except degreasing, by the removing
The sewage of grease successively passes through bacterial treatment, obtains eutrophic water；The eutrophic water is handled using aquatic animals and plants, is obtained
Middle water；Grease is transported in following combustion chambers by oil rig and goes to burn；
The mud of bottom in garbage pool is handled by mud press-forming units, that is, is collected, is crushed, it is clear with clear water
It after washing, dries, dries, add the loess of 2 times of weight or isometric concrete is added being formed with molding machine, obtain molding building materials；
Product, organic gas and grease that the solid content press-forming units are handled are delivered to combustion chamber to carry out
Burning, the burning use mass fraction for 99% oxygen, and the temperature of burning is 2000 DEG C；
The molding building materials that sludge molding cell processing obtains are delivered to calcining compartment to calcine, the temperature of calcining is 700
DEG C, obtain the calcined product that can be used as brickmaking building materials raw material.
The embodiment of the present invention 1 provide refuse disposal system rubbish can be realized it is innoxious, and without any need fill
Residue.
Embodiment 2
It is cylindrical body, overall diameter by shapeInterior diameterAerial part height 6m,
Lower Partial Height 2m, the collecting pit that liner material is stainless steel collect rubbish, are sent into, are sent into 100 tons of scales of dry matter daily
In addition to gravity flows naturally, it is 60m × 60m × 3m that the mode for increasing water flow, which is transported to specification, and dischargeable capacity is about 5000m3's
In airtight garbage pool, and the sewage that municipal sewage net obtains is conveyed together with the water flow and rubbish that are not less than 100 ton/hours
Into airtight garbage pool, in airtight garbage pool, by using mass fraction to be aerated at 25 DEG C for 99.9% or more nitrogen
Processing 4 hours or more, pressure when nitrogen is aerated was 0.5MPa, obtained gas, sewage, solid content and mud；Aeration terminates
Afterwards, the top of airtight garbage pool is cleaned everywhere using following middle water；
When above-mentioned nitrogen charged pressure is not less than 0.4MPa, starts air compressor machine, deliver the gas to gas treatment
In unit, compression separating treatment is carried out using air compressor machine, the pressure for compressing separation is 1.3MPa, obtains organic gas and inorganic gas
Body is collected by compression and is stored to air collector, then burnt by Pipeline transport into combustion chamber；The organic gas includes
Overflow carbonaceous organic material in closed pond；Nitrogen and other inorganic gas in gas meet national discharge through environmental monitoring instrument detection
It is discharged after standard GB14554-93 " emission standard for odor pollutants " is qualified；
Solid content is transported in specified cold sink using fishing slag slag conveyer, after being cleaned with clear water, is transported to solid content
Press-forming units are handled: it uses squeezing machine to squeeze out to rubbish water content and is dried after 10%~25%, to send to drying room,
It is crushed again with pulverizer after drying, it is spare to be sent into Bunker stacking, then be delivered to combustion chamber and burn；
Sewage transport is handled into grease pond, respectively obtains the sewage and grease except degreasing, by the removing
The sewage of grease successively passes through bacterial treatment, obtains eutrophic water；The eutrophic water is handled using aquatic animals and plants, is obtained
Middle water；Grease is transported in following combustion chambers by oil rig and goes to burn；
The mud of bottom in garbage pool is handled by mud press-forming units, that is, is collected, is crushed, it is clear with clear water
After washing, 2 tons of loess brickmaking binding materials are added with drying sewage sludge per ton；The mass ratio of the mud and loess is 1:2, with molding
Machine molding obtains molding building materials；
Product, organic gas and grease that the solid content press-forming units are handled are delivered to combustion chamber to carry out
Burning, the burning use mass fraction for 99% oxygen, and the temperature of burning is 2000 DEG C；
The molding building materials that sludge molding cell processing obtains are delivered to calcining compartment to calcine, the temperature of calcining is 700
DEG C, obtain the calcined product that can be used as building materials raw material.The calcined product is used as the raw material of brickmaking.
The embodiment of the present invention 2 provide refuse disposal system rubbish can be realized it is innoxious, and without any need fill
Residue.
As seen from the above embodiment, the present invention provides a kind of refuse disposal systems, including garbage collection unit；With it is described
The airtight rubbish unit of the garbage inlet connection of garbage collection unit, nitrogen aerator is equipped in the airtight rubbish unit,
For garbage disposal to be obtained gas, sewage, solid content and mud；The gas being connect with the gas vent of the airtight rubbish unit
Body processing unit, the air processing unit carry out the compression separation of gas；It is exported with the solid content of the airtight rubbish unit
The solid content press-forming units of connection；The precipitating oil removal unit being connect with the outlet of sewer of the airtight rubbish unit；With institute
State the drying pond of the sludge outlet connection of airtight rubbish unit；The biochemical treatment being connect with the precipitating oil removal unit by pipeline
Unit；The combustion chamber that the grease outlets of outlet and precipitating oil removal unit with the air processing unit are separately connected；With it is described
The calcining compartment of the outlet connection of solid content press-forming units.Rubbish can be realized nothing by refuse disposal system provided by the invention
Evilization, and the residue without any need landfill.
The above is only a preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art
For member, various improvements and modifications may be made without departing from the principle of the present invention, these improvements and modifications are also answered
It is considered as protection scope of the present invention.
Claims (5)
1. a kind of waste disposal method, comprising the following steps:
The rubbish that garbage collection unit is collected is transported to airtight rubbish unit, by nitrogen Air Exposure, obtains gas, dirt
Water, solid content and mud；The airtight rubbish unit includes airtight garbage pool, cleaning spray thrower and gas-tight door；The rubbish is received
Collection unit is connect by garbage shaft with airtight garbage pool；Rubbish is sent in garbage shaft using water flow mode；The gas
The temperature that nitrogen is aerated in close rubbish unit is 0 DEG C~40 DEG C；The time of nitrogen aeration is more than or equal to 4 hours；Nitrogen aeration
Pressure be more than or equal to 0.4MPa；
It delivers the gas to air processing unit to be handled, obtains organic gas；The air processing unit is using pressure
Division from mode, the isolated pressure of the compression is 0.5~1.4MPa；Solid content is transported at solid content drying unit
Reason；By sewage transport to precipitating oil removal cell processing, the sewage and grease except degreasing are respectively obtained, by described except degreasing
Sewage passes through biochemical treatment unit, obtains middle water, the biochemical treatment unit includes at bacterial treatment unit and aquatic animals and plants
Unit is managed, the entrance of the bacterial treatment unit is connect with the outlet of precipitating oil removal unit, the outlet of the bacterial treatment unit
It is connect with the entrance of aquatic animals and plants processing unit, the temperature of the biochemical treatment cell processing is 0 DEG C~50 DEG C；The biochemistry
The time of processing unit processes is for 24 hours~72h；Mud is transported to mud press-forming units to handle；
Product, organic gas and grease that the solid content drying unit is handled are delivered to combustion chamber to burn；
The product that mud press-forming units are handled is delivered to calcining compartment to calcine, obtains can be used as building materials raw material
Calcined product；The temperature of the calcining is 400 DEG C~1000 DEG C.
2. waste disposal method according to claim 1, which is characterized in that fishing slag slag conveyer is arranged in airtight rubbish unit
Solid content exit.
3. waste disposal method according to claim 1, which is characterized in that scraper plate slurry conveying machine is arranged in airtight rubbish list
At the sludge outlet of member.
4. waste disposal method according to claim 1, which is characterized in that the sewage inlet with the airtight rubbish unit
The cesspool of connection.
5. waste disposal method according to claim 1, which is characterized in that the burning is more than or equal to using mass fraction
99% oxygen；The temperature of the burning is 1200 DEG C~2000 DEG C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610707064.4A CN106269792B (en) | 2016-08-23 | 2016-08-23 | A kind of refuse disposal system and waste disposal method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610707064.4A CN106269792B (en) | 2016-08-23 | 2016-08-23 | A kind of refuse disposal system and waste disposal method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106269792A CN106269792A (en) | 2017-01-04 |
| CN106269792B true CN106269792B (en) | 2019-03-08 |
Family
ID=57614724
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610707064.4A Active CN106269792B (en) | 2016-08-23 | 2016-08-23 | A kind of refuse disposal system and waste disposal method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106269792B (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105032887A (en) * | 2015-06-26 | 2015-11-11 | 司伟东 | Ecological construction system for municipal garbage comprehensive disposal and utilization and disposal and utilization method |
| CN105457985A (en) * | 2015-12-25 | 2016-04-06 | 安徽继宏环保科技有限公司 | Dissolved air flotation machine of town domestic rubbish disposal system |
| CN105668937A (en) * | 2016-03-25 | 2016-06-15 | 胡志忠 | Ecological peristalsis bed reactor and method using same to treat waste water |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2005179509A (en) * | 2003-12-19 | 2005-07-07 | Matsushita Electric Ind Co Ltd | Method of heating |
| CN101318195A (en) * | 2008-04-30 | 2008-12-10 | 北京恒业村科技有限公司 | Wet separation classification processing and reutilization method for domestic garbage |
| KR100923032B1 (en) * | 2008-12-10 | 2009-10-22 | (주)이앤페트로테크놀러지 | Organic waste treatment system |
-
2016
- 2016-08-23 CN CN201610707064.4A patent/CN106269792B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105032887A (en) * | 2015-06-26 | 2015-11-11 | 司伟东 | Ecological construction system for municipal garbage comprehensive disposal and utilization and disposal and utilization method |
| CN105457985A (en) * | 2015-12-25 | 2016-04-06 | 安徽继宏环保科技有限公司 | Dissolved air flotation machine of town domestic rubbish disposal system |
| CN105668937A (en) * | 2016-03-25 | 2016-06-15 | 胡志忠 | Ecological peristalsis bed reactor and method using same to treat waste water |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106269792A (en) | 2017-01-04 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101524700B (en) | Treating technical method for food wastes and treating equipment | |
| CN103599920B (en) | A kind of solid-liquid separates and organic matter separates waste disposal method and device with inorganic matter | |
| CN201385040Y (en) | Food waste treatment equipment | |
| CN102690134A (en) | Processing method and processing system for kitchen garbage resourcilization | |
| CN109396161A (en) | The quick volume reduction decrement of crude waste and the method for comprehensive resource processing | |
| CN1850365A (en) | Garbage comprehensive treatment method and apparatus | |
| CN208151175U (en) | A kind of oily sludge harmless treatment device | |
| CN1164375C (en) | Urban garbage centralized treatment and regeneration method | |
| CN111389878A (en) | Domestic waste solid zero release processing system | |
| KR101339563B1 (en) | Apparatus for removing organic sludge | |
| CN201842753U (en) | Drying deice for utilization of urban sludge as resources | |
| KR20150088218A (en) | Pollutants contained in alcohol and milk, polluted rainwater and early stormwater and seawater and blood or fluidic symbols Fluid substances such as food or vinegar and soybeans Fluid substances constituting food or common fresh water Molecules and contaminated air Friendly and eco-friendly method that completely removes all binding substance molecules and floating substances combined with clean substances or mixes contaminant molecules extracted from fluid substance molecules with other substances and reuses or cleans them | |
| CN208712502U (en) | Waste density sorting machine and waste incineration pre-processing device | |
| CN101982532A (en) | System for preparing refuse derived fuel from high-calorific-value components of house refuse | |
| KR20150088214A (en) | Contaminated rainwater, initial rainwater, seawater, milk, liquor, blood, or fluidic sign Foods or fluid substances that are composed of fluid-like foods or common fresh water, such as vinegar and grains, Environment-friendly eco-friendly method that completely removes substances to purify cleanly or mix pollutant molecules extracted from fluid substance molecules with other substances and reuse or clean them. | |
| CN110899310A (en) | Perishable garbage pretreatment device and perishable garbage pretreatment method | |
| CN108687123A (en) | Waste density sorting machine, waste incineration pre-processing device and its method | |
| CN212069896U (en) | Domestic waste solid zero release processing system | |
| KR20150116431A (en) | Environment-friendly eco-friendly method of processing all kinds of fluids into molecules of fluids by separating and processing light fluids molecules in molecules | |
| CN106269792B (en) | A kind of refuse disposal system and waste disposal method | |
| CN113134501B (en) | Household garbage pretreatment system and method | |
| KR20150102888A (en) | All kinds of fluid substances that are configured to be consumed. Lightweight fluid substances contained in molecules. Separation and processing of molecules. Fluid substances useful for the human body. | |
| KR20150087162A (en) | Contaminated rainwater, initial rainwater, seawater, milk, liquor, blood, or fluidic sign Foods or fluid substances that are composed of fluid-like foods or common fresh water, such as vinegar and grains, Environment-friendly eco-friendly method that completely removes substances to purify cleanly or mix pollutant molecules extracted from fluid substance molecules with other substances and reuse or clean them. | |
| KR20150088212A (en) | Contaminant Molecules and Fluid Matter Nature-friendly fluidity that completely removes the particulate contaminants and suspended matter contained in the molecules or mixes the substance molecules extracted from the fluid substance molecules with other substances to reuse or clean them Material molecular processing eco-friendly method | |
| KR20150034159A (en) | Rainwater and early stormwater, fluid materials such as fresh water, seawater, milk, liquor and blood, all the bonding substances contained in the molecules and the particulate pollutants contained in the fluid material molecules, Fluid substances Molecules extracted from molecules Molecules mixed with other substances to reuse or purify Nature-friendly fluid materials Molecular processing Environmentally friendly methods |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20220826 Address after: 4th Floor, Office Building, R&D Center, Anhui Taiyuan Construction Machinery Co., Ltd., No. 530, Dangtu North Road, Xinzhan District, Hefei City, Anhui Province, 230000 Patentee after: Anhui zhongkedonggao Intelligent Technology Co.,Ltd. Address before: No. 16 China World Trade Center Road, Longhua District, Hainan, Jin Fucheng, Patentee before: Liu Chun |