CN104263388B - Rubbish carbonization reaction system - Google Patents
Rubbish carbonization reaction system Download PDFInfo
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- CN104263388B CN104263388B CN201410522166.XA CN201410522166A CN104263388B CN 104263388 B CN104263388 B CN 104263388B CN 201410522166 A CN201410522166 A CN 201410522166A CN 104263388 B CN104263388 B CN 104263388B
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- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 124
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 104
- 238000003763 carbonization Methods 0.000 title claims abstract description 41
- 239000000203 mixture Substances 0.000 claims abstract description 11
- 239000000446 fuel Substances 0.000 claims abstract description 10
- 239000002028 Biomass Substances 0.000 claims abstract description 9
- 230000008859 change Effects 0.000 claims abstract description 6
- 238000005859 coupling reaction Methods 0.000 claims abstract description 4
- 230000035484 reaction time Effects 0.000 claims abstract description 4
- 238000001035 drying Methods 0.000 claims description 29
- 238000012216 screening Methods 0.000 claims description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 23
- 239000007788 liquid Substances 0.000 claims description 16
- 238000012545 processing Methods 0.000 claims description 13
- 238000003860 storage Methods 0.000 claims description 13
- 239000004033 plastic Substances 0.000 claims description 8
- 229920003023 plastic Polymers 0.000 claims description 8
- 239000007787 solid Substances 0.000 claims description 8
- 238000009413 insulation Methods 0.000 claims description 7
- 238000012360 testing method Methods 0.000 claims description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 6
- 238000000151 deposition Methods 0.000 claims description 6
- 238000007789 sealing Methods 0.000 claims description 6
- 238000007493 shaping process Methods 0.000 claims description 4
- 229910052742 iron Inorganic materials 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- 238000002485 combustion reaction Methods 0.000 abstract description 5
- 239000007789 gas Substances 0.000 description 42
- 238000000034 method Methods 0.000 description 20
- 230000008569 process Effects 0.000 description 15
- 239000003245 coal Substances 0.000 description 13
- 239000002699 waste material Substances 0.000 description 12
- 238000011161 development Methods 0.000 description 10
- 238000010276 construction Methods 0.000 description 9
- 230000007613 environmental effect Effects 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 8
- 239000002920 hazardous waste Substances 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 7
- 239000002361 compost Substances 0.000 description 6
- 239000002689 soil Substances 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000007726 management method Methods 0.000 description 5
- 229910001385 heavy metal Inorganic materials 0.000 description 4
- 230000007547 defect Effects 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical group O1C=COC=C1 KVGZZAHHUNAVKZ-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
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 239000010425 asbestos Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000010791 domestic waste Substances 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 239000003673 groundwater Substances 0.000 description 2
- 230000008676 import Effects 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 230000002441 reversible effect Effects 0.000 description 2
- 229910052895 riebeckite Inorganic materials 0.000 description 2
- 239000005028 tinplate Substances 0.000 description 2
- 238000004056 waste incineration Methods 0.000 description 2
- 206010003694 Atrophy Diseases 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 1
- 241000628997 Flos Species 0.000 description 1
- 241000700605 Viruses Species 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 1
- 230000037444 atrophy Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000002802 bituminous coal Substances 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 150000001722 carbon compounds Chemical class 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000002817 coal dust Substances 0.000 description 1
- 239000003653 coastal water Substances 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 238000009264 composting Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 description 1
- 238000009440 infrastructure construction Methods 0.000 description 1
- 238000001802 infusion Methods 0.000 description 1
- 238000007885 magnetic separation Methods 0.000 description 1
- 239000002906 medical waste Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000010815 organic waste Substances 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000005180 public health Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000009183 running Effects 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/46—Solid fuels essentially based on materials of non-mineral origin on sewage, house, or town refuse
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Combustion & Propulsion (AREA)
- Processing Of Solid Wastes (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
Abstract
The invention provides a kind of rubbish carbonization reaction system and include reactor, reaction chamber, steam generator and control device；Wherein, steam generator coupled reaction still, described steam generator is for providing steam to described reactor；Described reaction chamber is used for placing rubbish, when reacted, described reaction chamber pushes the reaction of described reactor and generates carbonized mixture；After reaction completes, described reaction chamber is pulled out from described reactor.Described reactor includes kettle and kettle cover；Described kettle is tightly connected with described kettle cover；Described control device connects described reactor, and described control device is for controlling pressure and the change of temperature and reaction time in described reactor；The first guide rail of the length direction extension along described kettle it is provided with in kettle.Present configuration scheme is reasonable, equipment is advanced, automaticity is high, equipment investment cost is low, required area of mill site is little, and the biomass fuel combustion value prepared is high, it is low to discharge.
Description
Technical field
The present invention relates to technical field of domestic garbage treatment, in particular it relates to a kind of rubbish carbonization reaction system.
Background technology
According to data, China's domestic waste average growth rate per annum is 8%～10%, domestic waste in 2013
Reaching 2.6 hundred million tons, the rural area house refuse whole year the nearlyest hundred million tons, the house refuse grown with each passing day has become puzzlement economy and has sent out
Exhibition and the significant problem of environmental improvement.To this, country and local governments at various levels pay much attention to, and China newly puts into effect in recent years
A series of new policy and new planning, make policy to garbage disposal problem and practicality illustrate comprehensively, especially
Being " 12 " period, field of Environment Protection and waste management are formulated great planning, for China's house refuse by country
Processing item provides important development opportunity.Meanwhile, " 18 is big " clearly proposes " conservation culture ", " U.S.
Beautiful China ", " economizing on resources ", the content such as " protection environment ", this creates the biggest also to garbage disposal industry
Development space.The master file relating to garbage disposal at present has:
1. on April 19th, 2012, the General Office of the State Council printed and distributed " " 12 " whole nation application of city life garbage without
Evilization treatment facility construction plan " (Office of the State Council sends out [2012] No. 23), this planning is by State Development and Reform Commission, house town and country
The Ministry of Construction, the united organization establishment of Environmental Protection Department three ministries and commissions, illustrate " 12 " whole nation in period urban life rubbish
Target, main task and the safeguard of rubbish harmless treatment Facilities Construction, specifies the focus of government work.This is me
The programmatic document that state's Municipal Solid-state Garbage-disposal Facilities is built, planning construction gross investment 263,600,000,000 yuan.
2. on June 16th, 2012, State Council has printed and distributed " " 12 " energy-conserving and environment-protective industrial development planning " (state
Send out [2012] No. 19), relate to the content of the aspects such as technical equipment, energy-conserving product, energy-conserving and environment-protective service, especially
It is in major fields, be expressly mentioned renewable resource utilization, the side such as kitchen castoff recycling and garbage disposal
The related content in face.
3. on July 9th, 2012, State Council has printed and distributed " " 12 " national strategy new industry development plan "
(promulgated by the State Council [2012] 28), proposes the advanced environmental protection industry of development, in promoting rubbish and hazardous waste process disposal etc.
Hold；Development resource recycles industry, gives priority to the waste and old commodity recovery system supported with advanced technology, kitchen
The contents such as discarded object, agriculture and forestry organic waste material, waste textile and waste or used plastics goods recycling.
4. on August 6th, 2012, State Council has printed and distributed and " has planned about " 12 " printing and distributing energy-saving and emission-reduction
Notice " (promulgated by the State Council [2012] 40), propose to strengthen town environment infrastructure construction；Implement rural area cleaning project,
Encouraging categorized consumer waste to collect and decrement harmless treatment on the spot, selection is economical, be suitable for, safe process is disposed
Technology, improves rubbish processing to be harmless level, and Urban-rural integrated is progressively promoted in the rural area of cities and towns periphery and environmental sensitive area
Change garbage disposal pattern；Accelerating application of city life garbage and process disposal facility construction, strengthening percolate is disposed；Add
Strong policy is implemented and guides, and encourages to use Energy Management Contract to implement reducing energy consumption, promotes at town sewage, rubbish
Environmental protection facility socialization, the specialized runnings such as reason and enterprise pollution improvement.
5. on October 8th, 2012, Environmental Protection Department, National Development and Reform Committee, Ministry of Industry and Information, the associating of ministries and commissions of the Ministry of Public Health four
Print and distribute " " 12 " Hazardous Wastes Management control program " (environment-development [2012] 123), it is proposed that carry out
Hazardous waste is investigated, and tries to explore hazardous waste Sources decreasing, plans as a whole to advance dangerous waste incineration, landfill etc. to concentrate
Disposal facility is built, and scientific development hazardous waste utilizes and service industry, strengthens relating to heavy metal hazardous waste innoxious
Utilize and dispose, advance clinical waste harmlessness disposing, promote non-industrial source and left over by history hazardous waste to utilize and dispose,
Promote operation management and technical merit, strengthen the 9 big tasks such as hazardous waste supervisory system construction.
According to these public documents above-mentioned, can gem-pure see, garbage disposal has become country and has attached great importance to
Technical field, but simultaneously we it also seen that at present technology of garbage disposal there is also a lot of deficiency, drawback and technology
Blank.
Make a general survey of other countries of the world, garbage disposal equally exist the severeest problem, especially developing country with
The most poor and backward country, the problems such as sanitary fill such as mountain, environmental pollution are serious become increasingly conspicuous, and need employing section badly
Learn, method efficient, environmental protection processes rubbish.
Waste disposal method mainly includes burning disposal, sanitary landfills, sorting compost at present.Burning disposal and health
Landfill not only ratio is great, also in the gesture being gradually increasing, and sorts compost gradually atrophy, and on the other hand, country is a surname
Passing and having little effect in terms of propelling refuse classification process, this all makes garbage disposal difficulty strengthen.It is the most prominent,
Rubbish is focused on by prior art and all there is many defects, continue to cause secondary pollution, rubbish to burn to environment
The addressing burning factory more adversely affects to social stability.Conventional garbage processing method is primarily present following defect and asks
Topic:
(1) burning disposal
1, gas discharge, causes secondary pollution
Burning mode is used to process rubbish, it usually needs to add the coal of auxiliary fuel, such as 5-10%, not only increase
Cost, adds the discharge of carbon monoxide, sulfur dioxide simultaneously, additionally produces multiple harmful gas especially in burning
Body, causes secondary pollution to environment.What wherein effect on environment was the most prominent is dioxin, the toxicity of dioxin
Very big, it is 130 times of cyanide, 900 times of arsenic, has the title of " poison in century ".Meanwhile, rubbish burns
Burning factory and all there is the problem that whole plant area stinks to high heaven, also having the regular air environment of periphery obviously affects.
Exactly because incineration treatment of garbage has the most serious impact, recent China Foshan, Zhejiang to surrounding enviroment
The area such as Hangzhou there occurs the Mass disturbance of a lot of mass protest government building waste incineration project, and impact is extremely disliked
Bad.
2, combustion residue, still needs to take up an area landfill
Burning disposal rubbish can produce the combustion residue of 20%-25%, and prior art is typically innoxious for residue place
After reason extruded and fill, this is still to occupy a large amount of soil.Owing to residue being harmful to other containing heavy metal
Material, treatment technology requires high, processing equipment complexity, processing cost height, if some incineration plant can not be fully
Residue carries out harmless treatment or processes not thorough, and this causes serious pollution by giving again soil, underground water.
3, enormous investment, economy return is little
Burning disposal rubbish needs enormous investment, and a year processes the incineration plant of 300,000 tons of rubbish to be needed to invest 3.2
Hundred million-3.5 hundred million, it is mainly used in buying large-area soil, complicated equipment, discharges in particular for harmless treatment
The equipment investment of gas and combustion residue is big, technical sophistication, and the 50% of total investment for construction to be reached, this causes
Project cost height, length return period, reduce the economic benefit of the project implementation.More having indivedual enterprise is that interests are not selected
Means reduce the investment of these processing equipments and do not reach the effect of harmless treatment, healthy to surrounding enviroment and the common people
Bring very big hidden danger.
(2) sanitary landfills
Garbage loading embeading its by rubbish is concentrated and is stacked or in directly placing into the soil, rubbish is not carried out harmless
Change processes, and remains the hidden danger such as substantial amounts of bacterium, virus, heavy metal pollution and imbeds underground in the lump；Its rubbish seepage
Liquid can permanent ground contamination groundwater resources, some areas are built landfill yard in seashore, are made to coastal waters water and marine organisms
Become harm.Garbage loading embeading not only wastes the land resource needed for a large amount of landfill, and the environmental pollution caused, due to
Land pollution has disguise, hysteresis quality, and has accumulation property, inhomogeneities, it is most important that have difficult reversible
Property, such as heavy metal is difficult to degrade and causes land pollution is substantially the process that can not reverse completely, organic pollution
Being also required to the long period could degrade, and this all brings infinite future trouble to descendants.The most many developed countries are bright
Landfill waste is forbidden in order.The authorities at different levels of the Chinese government and technical specialist all think that this kind of mode processes rubbish not
Can persistently, but not yet find one i.e. to prevent the pollution of the environment, again the processing mode of high-efficient simple replace this type of and process
Mode.
(3) sorting compost
Garbage sorting compost is made by the ability of microbial decomposition, is decomposed by the organic matter in rubbish, at compost
After reason, become Crop fertilizer, and inorganic metal object therein and glass, fragment of brick etc. are filled, rubber
Plastics etc. then reclaim；But consumer garbage compost amount is big, the content of nitrogen and phosphorous is low, Long-Time Service easily cause soil compaction and
Groundwater quality degenerates, and the most also has following distinct issues: 1, odor pollution；2, operating cost is too high；3、
Technology is immature；4, factory management is bad etc., so garbage sorting composting technology is the most immature.
Through prior art retrieval is found Application No. 201320221711.2, patent name is that a kind of integral type utilization is useless
Expecting the utility model of device for coal processed, this utility model includes coal making machine main body, and is arranged on coal making machine body interior
Shaping mold cavity, and it is arranged on the stir storehouse of coal making machine body top, and it is arranged on the waste material charge door on the left of stir storehouse,
And it is arranged on the powder coal charge mouth on the right side of stir storehouse, and it is arranged on the motor at stir storehouse top, and it is arranged on stir storehouse
The internal mixer being connected with motor output shaft, and it is arranged on the outlet on the coal making machine main body left side, and it is arranged on system
Import on the right of coal owner's body, and be arranged on the drying machine on the left of outlet, and through import, outlet and drying machine,
For transporting the conveyer belt of readymade coal, between described coal making machine main body and stir storehouse, it is provided with an inlet valve, described coal processed
The outside of owner's body is provided with an inlet valve and controls switch.But this utility model is only limitted to use waste material for building
It is mixed and made into readymade coal, it is impossible to be applicable to the reaction coal of house refuse with coal dust.
Summary of the invention
For defect of the prior art, it is an object of the invention to provide a kind of rubbish carbonization reaction system.
Reactor, steam generator and control device is included according to the rubbish carbonization reaction system that the present invention provides, wherein,
Described control device connect described reactor, steam generator coupled reaction still, described steam generator for described instead
Answering still to provide steam, described reactor is for generating carbonized mixture by rubbish reaction.
Described control device is for controlling pressure and the change of temperature and reaction time in described reactor.
Preferably, described reactor includes kettle and kettle cover；Described kettle cover is used for sealing described kettle；Set on described kettle
It is equipped with gas access port, gas discharge outlet, condensate drain mouth, pressure test mouth and temperature test mouth；
The first guide rail of the length direction extension along described kettle it is provided with in described kettle.
Preferably, also include that multiple reaction chamber, described reaction chamber are used for placing rubbish, when reacted, by described reaction chamber
Push reactor, after reaction completes, described reaction chamber is pulled out from described reactor.
Preferably, support is also included；
The second guide rail it is provided with on the upside of described support；The bottom of described reaction chamber is provided with and the second rail brackets and first
The roller that frame all coordinates.
Preferably, drying unit, the first screening plant and shaped device are also included；
Wherein, described drying unit is used for drying described carbonized mixture；
Described first screening plant is for going out screening substances incombustible in carbonized mixture after drying, thus obtains carbon
Compound；
Described shaped device sets the shaping biomass fuel of shape for being processed into by carbide.
Preferably, gas storage case and/or pneumatic filter are also included；
Described gas storage case connects described gas discharge outlet；Described pneumatic filter connects described gas storage case；
Described gas storage case generates gas when being used for depositing reaction；Described pneumatic filter is used for purifying described gas.
Preferably, also including aqueous water receptacle and/or aqueous water processing means, described aqueous water receptacle connects described
Condensate drain mouth, the liquid generated during for depositing reaction；Described aqueous water processing means connects described aqueous water and deposits
Device, the purified treatment of the liquid generated in time reacting.
Preferably, concentration equipment and/or the second screening plant are also included；Described concentration equipment, described second screening plant
And described reaction chamber is sequentially disposed adjacent；
Described concentration equipment removes the iron block in rubbish before rubbish is put into reaction chamber；Described second screening plant is used for
Remove the plastic garbage in rubbish further.
Preferably, equipment for separating liquid from solid and/or drying device are also included；Described equipment for separating liquid from solid and described drying device
It is sequentially arranged between described second screening plant and described reaction chamber
Described equipment for separating liquid from solid is for removing the moisture in rubbish further by the rubbish removing plastic garbage；Described dry
Device is for drying the rubbish removing moisture removal further.
Preferably, also include that double-spiral feeder, described double-spiral feeder are arranged on described reaction chamber and described dry dress
Between putting；
Described double-spiral feeder rubbish after drying loads described reaction chamber.
Preferably, multiple reaction chambers join end to end in described reactor in linear array or multiple reaction chamber is in described reaction
Still is arranged side by side.
Preferably, described gas access port includes the first gas access port and the second gas access port；
Wherein, the first gas access port is arranged on the downside of described kettle and near described kettle centre position；Described second
Gas access port is arranged on the seal head end of described kettle；
First gas access port and the second gas access port are all connected with described steam generator.
Preferably, described condensate drain mouth includes the first condensate drain mouth and the second condensate drain mouth；
Wherein, described first condensate drain mouth is arranged on the downside of described kettle and near described kettle centre position；Institute
State the second condensate drain mouth and be arranged on downside and the end of sealing up a door of close described kettle of described kettle；
First condensate drain mouth and the second condensate drain mouth are all connected with described aqueous water receptacle.
Preferably, also include that insulation part, described insulation part are arranged on the outside of described kettle.
Preferably, also including safety valve and relief valve connection, described safety valve connects described still by described relief valve connection
Body.
Preferably, also include that jacking system, described jacking system are arranged on inside described support, described jacking system 25
Connect the downside of described casing, be used for driving described casing.
Preferably, described jacking system includes that push rod, the downside of described casing are provided with two holes that are relatively fixed with fixing
Axle, the end of described push rod is provided with connecting hole；
Described fixing axle inserts described connecting hole and described jacking system and described casing are linked together by described fixing hole.
Preferably, the side of described box bottom is provided with the first rotating shaft 27；The side of the upper surface of described support is provided with
The axle sleeve matched with described first rotating shaft；
When casing described in described jacking system jack-up, described casing is along described first axis of rotation.
Preferably, casing includes the first side plate, the second side plate and the second rotating shaft；
The two ends of described first side plate are connected with the two ends of described casing by the second rotating shaft respectively；
Corresponding described second side plate of described first side plate.
Preferably, also include that osculum, described osculum are arranged on the first side plate of described casing and the second side plate and institute
State the osculum bottom near described casing；
Wherein, the osculum being arranged on described first side plate and the osculum being arranged on described second side plate are at same axle
On line.
Compared with prior art, the present invention has a following beneficial effect:
(1) refuse classification is required low by the present invention, and nearly all house refuse all can process；
(2) automaticity of the present invention is high, after a upper operation completes, monitors according to dynamic state of parameters, can automatically enter
Enter subsequent processing, therefore operating cost economy, meet very much innoxious, the resource of garbage disposal, industrialization is sent out
Exhibition direction；
(3) the whole production system of the present invention is discharged without foul smell, will not surrounding environment pollute；In production process
High temperature in reactor can effectively kill the germ in rubbish；The liquefaction water of formation, gas in production process, only
Need to by simple water treatment facilities and gas purifying equipment, can be formed may conform to national standard, can discharge
Water and gas, will not produce secondary pollution；
(4) the biomass fuel combustion value that present invention production obtains is higher, according to different rubbish kinds, burning
Value is 4500-6500 kilocalorie；
(5), in production process of the present invention, carbonized mixture obtains carbide by screening and is about described carbonization mixing
The 90% of thing, the present invention utilizes rubbish to produce the utilization rate additive method far above prior art of biomass fuel powder,
The rubbish of the overwhelming majority can be converted into carbide by the most whole production process, and the most less not carbonaceous component
Material can be discharged by screening；
(6) biomass fuel that the present invention generates, the discharge after burning is based on a small amount of carbon dioxide, and burn cigarette
Gas discharge capacity 50%-60% lower than common bituminous coal；
(7) the biomass fuel powder that the present invention generates, as the raw material of carbon fertilizer, thus can widen further
The purposes that garbage reclamation utilizes；
(8) the required infusion of financial resources of the construction project of the inventive method is few, and return is fast, because technique is simple, and equipment
Without complex appts, process the rubbish charing equipment of 300,000 tons of rubbish and the work that forms a complete production network a year so building
Factory, about needs to put into 50,000,000 yuans, about two years payoff periods, is the investment of equal treating capacity garbage burning factory
About 15%；
(9) technical solution of the present invention is reasonable, and equipment is advanced, and required area of mill site is little, builds and processes in a year
The factory that rubbish is 300,000 tons, it is only necessary to the soil of about 100 mu, and the garbage burning factory building equal treating capacity needs
400-500 mu；
(10) economy of the present invention, efficiently environmental issue and energy problem are organically combined, on industrialization height
Solving social enviroment protection problem, comply fully with the policy guidance of country, the market demand is the hugest simultaneously, according at present
Rubbish increment from the point of view of, at least need to build the garbage burning factory of 300,000 tons of scales of family more than 1000, use this skill
Art construction biomass fuel processing plant, at least can build about 100, institute before 2016 at home
It is the strong propelling to national environmental protection policy with this project implementation, is also the practicing to China's dream, there is important society
Can meaning.
Accompanying drawing explanation
By the detailed description non-limiting example made with reference to the following drawings of reading, the further feature of the present invention,
Purpose and advantage will become more apparent upon:
Fig. 1 is the structural representation of the present invention；
Fig. 2 is a kind of structural representation of reactor in the present invention；
Fig. 3 is the another kind of structural representation of reactor in the present invention；
Fig. 4 is a kind of structural representation of reaction chamber in the present invention；
Fig. 5 is the another kind of structural representation of reaction chamber in the present invention.
In figure:
1 is that waste deposit storehouse is or/and waste deposit is cheated；
2 is reaction chamber；
3 is reactor；
4 is gas storage case；
5 is pneumatic filter；
6 is steam generator；
7 is aqueous water receptacle；
8 is cistern or/and sewage network；
9 is drying unit；
10 is the first screening plant；
11 is shaped device；
12 is the first gas discharge outlet；
13 is relief valve connection；
14 is ventilation interface；
15 is pressure test mouth；
16 is temperature test mouth；
17 is the second gas discharge outlet；
18 is the first condensate outlet；
19 is the first gas access port；
20 is the first guide rail；
21 is casing；
22 is support；
23 is roller；
24 is the second guide rail；
25 is jacking system；
26 is axle sleeve；
27 is the first rotating shaft；
28 is the first side plate；
29 is the second rotating shaft；
30 is osculum.
Detailed description of the invention
Below in conjunction with specific embodiment, the present invention is described in detail.Following example will assist in those skilled in the art
Member is further appreciated by the present invention, but limits the present invention the most in any form.It should be pointed out that, the common skill to this area
For art personnel, without departing from the inventive concept of the premise, it is also possible to make some deformation and improvement.These broadly fall into
Protection scope of the present invention.
In the present embodiment, the rubbish carbonization reaction system that the present invention provides includes reactor 3, reaction chamber 2 and steam
Generator 6 and control device；
Wherein, described control device connects described reactor 3, and steam generator 6 coupled reaction still 3, described steam is sent out
Raw device 6 is for providing steam to described reactor 3；Described control device is used for controlling pressure and temperature in described reactor 3
The change of degree and reaction time.
Described reaction chamber 2 is used for placing rubbish, when reacted, described reaction chamber 2 pushes described reactor 3 by rubbish
Reaction generates carbonized mixture；After reaction completes, described reaction chamber 2 is pulled out from described reactor 3.Reactor
The pressure that can bear is more than 500 DEG C more than 35bar, temperature.
Wherein, in a kettle., before general reaction in the time period of 1/4-1/3, temperature in the range of 150 DEG C-250 DEG C,
Pressure is in the range of 15bar-25bar；After general reaction in the time period of 2/4-1/3, temperature is in the range of 200 DEG C
-500 DEG C, pressure is in the range of 20bar-35bar；In the middle of general reaction in the time period of 1/4-1/3, the model of temperature
To enclose be 150 DEG C-300 DEG C, and pressure is in the range of 18bar-25bar.
Described reactor 3 includes kettle and kettle cover；Described kettle cover is used for sealing described kettle；If being provided with on described kettle
Dry individual gas access port, several gas discharge outlet, several condensate drain mouths and several temperature test mouths；
The first guide rail of the length direction extension along described kettle it is provided with in described kettle.
The rubbish carbonization reaction system that the present invention provides also includes support；The second guide rail it is provided with on the upside of described support；Described
The bottom of reaction chamber 2 is provided with the roller all coordinated with the second rail brackets and the first support.
The rubbish carbonization reaction system that the present invention provides also includes drying unit the 9, first screening plant 10 and shaped device
11；
Wherein, described drying unit 9 is used for drying described carbonized mixture；Described first screening plant 10 will be for drying
After dry, in carbonized mixture, incombustible screening substances goes out, thus obtains carbide；
Described shaped device 11 for being processed into the shaping biomass fuel setting shape by carbide.
The rubbish carbonization reaction system that the present invention provides also includes gas storage case 4 and/or pneumatic filter 5；Described gas
Storage box 4 connects the first gas discharge outlet 12 and the second gas discharge outlet 17；Described pneumatic filter 5 connects institute
State gas storage case 4；Described gas storage case 4 generates gas when being used for depositing reaction；Described pneumatic filter 5 is used for
Purify described gas.
The rubbish carbonization reaction system that the present invention provides also includes that aqueous water receptacle 7, described aqueous water receptacle 7 connect
Described condensate drain mouth, the liquid generated during for depositing reaction.Described aqueous water processing means connects described aqueous water
Receptacle 7, the purified treatment of liquid generated in time reacting, and then enter cistern or/and sewage network 8.
The rubbish carbonization reaction system that the present invention provides also includes concentration equipment and/or the second screening plant；Described magnetic separation fills
Put, described second screening plant and described reaction chamber 2 are sequentially disposed adjacent.
Described concentration equipment removes the iron block in rubbish before rubbish is put into reaction chamber；Described second screening plant is used for
Remove the plastic garbage in rubbish further.
The rubbish carbonization reaction system that the present invention provides, also includes equipment for separating liquid from solid and/or drying device；Described solid-liquid
Separator and described drying device are sequentially arranged between described second screening plant and described reaction chamber 2；Described solid
Liquid separating apparatus is for removing the moisture in rubbish further by the rubbish removing plastic garbage；Described drying device be used for into
The rubbish removing moisture removal is dried by one step.
The rubbish carbonization reaction system that the present invention provides also includes that double-spiral feeder, described double-spiral feeder are arranged on institute
State between reaction chamber 2 and described drying device；
Described double-spiral feeder rubbish after drying loads described reaction chamber 2.Multiple reaction chambers 2 join end to end
In linear array or multiple reaction chamber 2 is arranged side by side in described reactor in described reactor.
Described gas access port includes the first gas access port 19 and the second gas access port；
Wherein, the first gas access port 19 is arranged on the downside of described kettle and near described kettle centre position；Described
Second gas access port is arranged on the seal head end of described kettle.
Described condensate drain mouth includes the first condensate drain mouth 18 and the second condensate drain mouth 17；Described condensation
Thing floss hole is used for discharging condensate in still；Wherein, described first condensate drain mouth 18 is arranged under described kettle
Side and close described kettle centre position；Described second condensate drain mouth 17 is arranged on the upside of described kettle and close
The end of sealing up a door of described kettle.
Rubbish carbonization reaction still in the present invention also includes that insulation part, described insulation part are arranged on the inner side of described kettle.Institute
State asbestos and tinplate that insulation part includes being fitted and connected；Described tinplate connects described kettle by described asbestos.This
Rubbish carbonization reaction still in bright also includes safety valve and relief valve connection 13, and described safety valve passes through described relief valve connection
13 connect described kettle.
Rubbish carbonization reaction case in the present invention also includes that jacking system 25, described jacking system 25 are arranged on described support
Inside 22, described jacking system 25 connects the downside of described casing 21, and described jacking system 25 is used for driving described case
Body.
Described jacking system 5 includes that push rod, the downside of described casing 1 are provided with two be relatively fixed hole and fixing axles,
The end of described push rod is provided with connecting hole；Described fixing axle inserts described connecting hole and described jack-up is filled by described fixing hole
Put 25 and described casing 21 link together.The side of described casing 21 base plate is provided with the first rotating shaft 27；Described
The side of frame 22 upper surface is provided with the axle sleeve 26 matched with described first rotating shaft 27；When described jacking system 25 pushes up
When playing described casing 21, described casing 21 rotates along described first rotating shaft 7.
Casing 21 includes the first side plate the 28, second side plate and the second rotating shaft 29；The two ends of described first side plate 28 are respectively
It is connected by the two ends of the second rotating shaft 29 with described casing 21；Corresponding described second side plate of described first side plate 28.The
The lower end of side plate 28 not base plate with described casing 21 is connected.
Rubbish carbonization reaction case in the present invention also includes that osculum 30, described osculum 30 are arranged on described casing 1
On first side plate 28 and the second side plate；Described osculum 30 is near the bottom of described casing 1；Wherein, described in being arranged on
Osculum 30 on first side plate 8 is with the osculum 10 being arranged on described second side plate on the same axis.
Rubbish carbonization reaction case in the present invention also includes that leak preventing, the two ends of described leak preventing are separately positioned on first
Side plate 28 is connected with on the second side plate and with the hole wall of described osculum 30；Described leak preventing and described casing 21 end
There is between plate space.Thus the product that leak preventing is possible to prevent in casing spills, but in casing, water can be from described sky
Gap flows out.
The two ends of described casing 21 are provided with buckle.Such that it is able to by multiple casings 21 by bayonet connection together.
When the product in casing toppled over by the rubbish carbonization reaction case in invention, first jacking system 25 is from casing 21
Side jack-up casing 21, casing 21 so that along the first rotating shaft 27 to side rotate, the lower end of the first side plate 28 and base plate
Separating, product is poured out between the lower end and base plate of the first side plate 28.
Above the specific embodiment of the present invention is described.It is to be appreciated that the invention is not limited in
Stating particular implementation, those skilled in the art can make various deformation or amendment within the scope of the claims,
This has no effect on the flesh and blood of the present invention.
Claims (20)
1. a rubbish carbonization reaction system, it is characterised in that include reactor (3), steam generator (6) and control
Device processed；Wherein, the described control device described reactor of connection (3), steam generator (6) coupled reaction still (3),
Described steam generator (6) is for providing steam to described reactor (3), and described reactor (3) is for by rubbish
Reaction generates carbonized mixture；
Described control device is used for controlling pressure and the change of temperature and reaction time in described reactor (3)；
Wherein, in a kettle., before general reaction in the time period of 1/4-1/3, temperature in the range of 150 DEG C-250 DEG C,
Pressure is in the range of 15bar-25bar；After general reaction in the time period of 2/4-1/3, temperature is in the range of 200 DEG C
-500 DEG C, pressure is in the range of 20bar-35bar；In the middle of general reaction in the time period of 1/4-1/3, the model of temperature
To enclose be 150 DEG C-300 DEG C, and pressure is in the range of 18bar-25bar.
Rubbish carbonization reaction system the most according to claim 1, it is characterised in that described reactor (3) includes
Kettle and kettle cover；Described kettle cover is used for sealing described kettle；Be provided with gas access port on described kettle, gas gives off
Mouth, condensate drain mouth, pressure test mouth and temperature test mouth；
The first guide rail of the length direction extension along described kettle it is provided with in described kettle.
Rubbish carbonization reaction system the most according to claim 2, it is characterised in that also include multiple reaction chamber (2),
Described reaction chamber (2) is used for placing rubbish, when reacted, described reaction chamber (2) is pushed reactor (3), when instead
After should completing, described reaction chamber (2) is pulled out from described reactor (3).
Rubbish carbonization reaction system the most according to claim 3, it is characterised in that also include support；
The second guide rail it is provided with on the upside of described support；The bottom of described reaction chamber (2) is provided with and the second guide rail and first
The roller that guide rail all coordinates.
Rubbish carbonization reaction system the most according to claim 1, it is characterised in that also include drying unit (9),
First screening plant (10) and shaped device (11)；
Wherein, described drying unit (9) is used for drying described carbonized mixture；
Described first screening plant (10) is used for screening substances incombustible in carbonized mixture after drying, thus
Obtain carbide；
Described shaped device (11) sets the shaping biomass fuel of shape for being processed into by carbide.
Rubbish carbonization reaction system the most according to claim 2, it is characterised in that also include gas storage case (4)
And/or pneumatic filter (5)；
Described gas storage case (4) connects described gas discharge outlet；Described pneumatic filter (5) connects described gas
Storage box (4)；
Described gas storage case (4) generates gas when being used for depositing reaction；Described pneumatic filter (5) is used for purifying institute
State gas.
7. according to the rubbish carbonization reaction system described in claim 2 or 6, it is characterised in that also include that aqueous water is deposited
Putting device (7) and/or aqueous water processing means, described aqueous water receptacle (7) connects described condensate drain mouth, uses
The liquid generated in time depositing reaction；Described aqueous water processing means connects described aqueous water receptacle (7), is used for reacting
The purified treatment of the liquid of Shi Shengcheng.
Rubbish carbonization reaction system the most according to claim 1, it is characterised in that also include concentration equipment and/or
Second screening plant；Described concentration equipment, described second screening plant and described reaction chamber (2) are sequentially disposed adjacent；
Described concentration equipment removes the iron block in rubbish before rubbish is put into reaction chamber；Described second screening plant is used for
Remove the plastic garbage in rubbish further.
Rubbish carbonization reaction system the most according to claim 8, it is characterised in that also include equipment for separating liquid from solid
And/or drying device；Described equipment for separating liquid from solid and described drying device be sequentially arranged at described second screening plant and
Between described reaction chamber (2)；
Described equipment for separating liquid from solid is for removing the moisture in rubbish further by the rubbish removing plastic garbage；Described dry
Device is for drying the rubbish removing moisture removal further.
Rubbish carbonization reaction system the most according to claim 9, it is characterised in that also include double-spiral feeder,
Described double-spiral feeder is arranged between described reaction chamber (2) and described drying device；
Described double-spiral feeder rubbish after drying loads described reaction chamber (2).
11. rubbish carbonization reaction systems according to claim 3, it is characterised in that multiple reaction chambers (2) are first
Tail is connected in described reactor in linear array mutually or multiple reaction chamber (2) is arranged side by side in described reactor.
12. rubbish carbonization reaction systems according to claim 2, it is characterised in that described gas access port includes
First gas access port (19) and the second gas access port；
Wherein, the first gas access port (19) is arranged on the downside of described kettle and near described kettle centre position；Institute
State the second gas access port to be arranged on the seal head end of described kettle；
First gas access port (19) and the second gas access port are all connected with described steam generator (6).
13. rubbish carbonization reaction systems according to claim 7, it is characterised in that described condensate drain mouth bag
Include the first condensate drain mouth (18) and the second condensate drain mouth；
Wherein, described first condensate drain mouth (18) is arranged on the downside of described kettle and near described kettle interposition
Put；Described second condensate drain mouth is arranged on downside and the end of sealing up a door of close described kettle of described kettle；
First condensate drain mouth (18) and the second condensate drain mouth (17) are all connected with described aqueous water receptacle (7).
14. rubbish carbonization reaction systems according to claim 2, it is characterised in that also include insulation part, described
Insulation part is arranged on the outside of described kettle.
15. rubbish carbonization reaction systems according to claim 2, it is characterised in that also include safety valve and safety
Valve interface (13), described safety valve connects described kettle by described relief valve connection (13).
16. rubbish carbonization reaction systems according to claim 4, it is characterised in that also include jacking system (25),
Described jacking system (25) is arranged on described support (22) inner side, and described jacking system (25) connects casing (21)
Downside, be used for driving described casing (21).
17. rubbish carbonization reaction systems according to claim 16, it is characterised in that described jacking system (25)
Including push rod, the downside of described casing is provided with two be relatively fixed hole and fixing axles, and the end of described push rod is provided with
Connecting hole；
Described fixing axle inserts described connecting hole and described fixing hole by described jacking system (25) and described casing (21)
Link together.
18. rubbish carbonization reaction systems according to claim 16, it is characterised in that the one of described box bottom
Side is provided with the first rotating shaft (27)；The side of the upper surface of described support is provided with the axle matched with described first rotating shaft
Set (26)；
When casing (21) described in described jacking system (25) jack-up, described casing rotates along described first rotating shaft (27).
19. rubbish carbonization reaction systems according to claim 4, it is characterised in that casing include the first side plate (28),
Second side plate and the second rotating shaft (29)；
The two ends of described first side plate (28) are connected with the two ends of described casing (21) by the second rotating shaft (29) respectively；
Corresponding described second side plate of described first side plate (28).
20. rubbish carbonization reaction systems according to claim 16, it is characterised in that also include osculum (30),
Described osculum (30) is arranged on the first side plate of described casing (21) and the second side plate and described osculum (30)
Bottom near described casing；
Wherein, the osculum being arranged on described first side plate (28) exists with the osculum being arranged on described second side plate
On same axis.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410522166.XA CN104263388B (en) | 2014-06-25 | 2014-09-30 | Rubbish carbonization reaction system |
| PCT/CN2014/092669 WO2016049978A1 (en) | 2014-06-25 | 2014-12-01 | Garbage carbonization reaction system |
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410293336.1 | 2014-06-25 | ||
| CN201410293336.1A CN104031713A (en) | 2014-06-25 | 2014-06-25 | Manufacturing method of pollution-free coal with high combustion value by household garbage |
| CN2014102933361 | 2014-06-25 | ||
| CN201410522166.XA CN104263388B (en) | 2014-06-25 | 2014-09-30 | Rubbish carbonization reaction system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104263388A CN104263388A (en) | 2015-01-07 |
| CN104263388B true CN104263388B (en) | 2016-08-17 |
Family
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410293336.1A Pending CN104031713A (en) | 2014-06-25 | 2014-06-25 | Manufacturing method of pollution-free coal with high combustion value by household garbage |
| CN201420575439.2U Expired - Lifetime CN204325226U (en) | 2014-06-25 | 2014-09-30 | Rubbish carbonization reaction system |
| CN201410522166.XA Active CN104263388B (en) | 2014-06-25 | 2014-09-30 | Rubbish carbonization reaction system |
| CN201410520612.3A Expired - Fee Related CN104403716B (en) | 2014-06-25 | 2014-09-30 | Method for producing biomass fuels by using garbage |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201410293336.1A Pending CN104031713A (en) | 2014-06-25 | 2014-06-25 | Manufacturing method of pollution-free coal with high combustion value by household garbage |
| CN201420575439.2U Expired - Lifetime CN204325226U (en) | 2014-06-25 | 2014-09-30 | Rubbish carbonization reaction system |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201410520612.3A Expired - Fee Related CN104403716B (en) | 2014-06-25 | 2014-09-30 | Method for producing biomass fuels by using garbage |
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| CN (4) | CN104031713A (en) |
| WO (3) | WO2015196502A1 (en) |
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| CN104031713A (en) * | 2014-06-25 | 2014-09-10 | 沙嫣 | Manufacturing method of pollution-free coal with high combustion value by household garbage |
| CN105219471B (en) * | 2015-10-17 | 2018-02-09 | 明光市龙腾矿物有限公司 | One kind contains sepiolite composite biomass fuel and preparation method thereof |
| CN105296046B (en) * | 2015-10-17 | 2017-12-08 | 明光市龙腾矿物有限公司 | A kind of biomass fuel containing calcareous shale |
| CN105598137B (en) * | 2016-02-22 | 2017-09-12 | 长沙雷邦环保科技有限公司 | A kind of solid waste integrated synthesis processing unit |
| CN106867616A (en) * | 2017-03-22 | 2017-06-20 | 合肥浦尔菲电线科技有限公司 | A kind of Novel environment-friendlymaterial material and preparation method thereof |
| CN109294600B (en) * | 2018-12-06 | 2024-01-23 | 黑龙江省能源环境研究院 | Multi-bin vertical biomass carbonization experiment furnace and application method thereof |
| CN110716479B (en) * | 2019-11-13 | 2022-06-03 | 河北星鼎机械设备制造有限公司 | Control method of garbage anaerobic carbonization system |
| CN114011841B (en) * | 2021-09-23 | 2022-08-12 | 中铁市政环境建设有限公司 | Distributed garbage carbonization treatment system |
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Also Published As
| Publication number | Publication date |
|---|---|
| CN104031713A (en) | 2014-09-10 |
| CN104263388A (en) | 2015-01-07 |
| WO2016049978A1 (en) | 2016-04-07 |
| CN104403716A (en) | 2015-03-11 |
| WO2015196502A1 (en) | 2015-12-30 |
| CN104403716B (en) | 2017-01-18 |
| WO2015196732A1 (en) | 2015-12-30 |
| CN204325226U (en) | 2015-05-13 |
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