CN106111667A - Biomass are prepared RDF 4 smokeless and are burned steam-electric power technique - Google Patents
Biomass are prepared RDF 4 smokeless and are burned steam-electric power technique Download PDFInfo
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- CN106111667A CN106111667A CN201610488760.0A CN201610488760A CN106111667A CN 106111667 A CN106111667 A CN 106111667A CN 201610488760 A CN201610488760 A CN 201610488760A CN 106111667 A CN106111667 A CN 106111667A
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- 238000000034 method Methods 0.000 title claims abstract description 21
- 239000002028 Biomass Substances 0.000 title claims abstract description 20
- 238000001035 drying Methods 0.000 claims abstract description 42
- 239000010813 municipal solid waste Substances 0.000 claims abstract description 33
- 239000000463 material Substances 0.000 claims abstract description 32
- 239000007789 gas Substances 0.000 claims abstract description 28
- 239000000446 fuel Substances 0.000 claims abstract description 19
- 239000002918 waste heat Substances 0.000 claims abstract description 18
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000003546 flue gas Substances 0.000 claims abstract description 16
- 230000008569 process Effects 0.000 claims abstract description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 8
- 239000001301 oxygen Substances 0.000 claims abstract description 8
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 8
- 239000002699 waste material Substances 0.000 claims abstract description 7
- 238000004659 sterilization and disinfection Methods 0.000 claims description 13
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 12
- 239000002245 particle Substances 0.000 claims description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 230000001954 sterilising effect Effects 0.000 claims description 10
- 239000011521 glass Substances 0.000 claims description 8
- 230000018044 dehydration Effects 0.000 claims description 6
- 238000006297 dehydration reaction Methods 0.000 claims description 6
- 239000002994 raw material Substances 0.000 claims description 6
- 238000012216 screening Methods 0.000 claims description 6
- 239000004033 plastic Substances 0.000 claims description 5
- 229920003023 plastic Polymers 0.000 claims description 5
- 238000009833 condensation Methods 0.000 claims description 4
- 230000005494 condensation Effects 0.000 claims description 4
- 239000011449 brick Substances 0.000 claims description 3
- 239000004566 building material Substances 0.000 claims description 3
- 238000004140 cleaning Methods 0.000 claims description 3
- 239000002361 compost Substances 0.000 claims description 3
- 238000005469 granulation Methods 0.000 claims description 3
- 230000003179 granulation Effects 0.000 claims description 3
- 229910052742 iron Inorganic materials 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 230000008929 regeneration Effects 0.000 claims description 3
- 238000011069 regeneration method Methods 0.000 claims description 3
- 239000002689 soil Substances 0.000 claims description 3
- 239000004575 stone Substances 0.000 claims description 3
- 238000005491 wire drawing Methods 0.000 claims description 3
- 230000008901 benefit Effects 0.000 abstract description 4
- 239000003500 flue dust Substances 0.000 abstract description 2
- 238000004064 recycling Methods 0.000 abstract description 2
- 238000001179 sorption measurement Methods 0.000 abstract description 2
- 238000012545 processing Methods 0.000 description 4
- 238000004332 deodorization Methods 0.000 description 2
- 239000010791 domestic waste Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 230000006872 improvement Effects 0.000 description 2
- 238000011160 research Methods 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
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000011953 bioanalysis Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000004035 construction material Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000010921 garden waste Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01D—NON-POSITIVE DISPLACEMENT MACHINES OR ENGINES, e.g. STEAM TURBINES
- F01D15/00—Adaptations of machines or engines for special use; Combinations of engines with devices driven thereby
- F01D15/10—Adaptations for driving, or combinations with, electric generators
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01K—STEAM ENGINE PLANTS; STEAM ACCUMULATORS; ENGINE PLANTS NOT OTHERWISE PROVIDED FOR; ENGINES USING SPECIAL WORKING FLUIDS OR CYCLES
- F01K11/00—Plants characterised by the engines being structurally combined with boilers or condensers
- F01K11/02—Plants characterised by the engines being structurally combined with boilers or condensers the engines being turbines
-
- 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)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention discloses biomass and prepare RDF 4 smokeless burning steam-electric power technique, it is that biomass through a series of process and are rolled and make powder-shaped rubbish derivatived fuel (RDF 4), burning RDF 4 bulk fuel also collects the produced high-temperature flue gas of burning, utilize high-temperature flue gas to pass through heat exchange and absorb generation vapours, vapours is passed into steam turbine generator and carries out steam-electric power.The waste heat gas produced during heat exchange absorbs is respectively used to drying garbage and RDF 4 burns in oxygen supply.Present invention achieves the comprehensive utilization of waste resource, play maximum economic benefit；The waste heat gas produced during residual heat boiler for exchanging heat is used for dried material rubbish, it is achieved recycling of heat energy；Flue dust in waste heat gas is played adsorption by material rubbish, and a part is dried produced gas and is passed in combustor, and burning for RDF 4 removes foul smell while oxygen supply.
Description
Technical field
The present invention relates to the processing technology field of biomass, particularly relate to a kind of biomass and prepare RDF-4 smokeless
Burn steam-electric power technique.
Background technology
Along with the fast development of China's economy, the domestic waste yield of China increases day by day, the process of rubbish and place
Put and have become as the problem that China big and medium-sized cities must solve；China's municipal refuse annual production is about to 1. 5 hundred million tons at present, and
The most also increasing；How to realize that domestic waste is innoxious, " three change " of minimizing and resource processes and has become research
Focus.House refuse is sorted, selects combustible constituent and roll and make powder-shaped rubbish derivatived fuel (RDF-4), burn and dissipate
Shape garbage derivatived fuel (RDF-4) is also collected by burning produced high-temperature flue gas, then high-temperature flue gas is passed into waste heat boiler
Producing vapours, the technical scheme those skilled in the art then utilizing vapours to carry out steam-electric power have been carried out research,
And achieve praiseworthy technological achievement.
Above house refuse is made bulk fuel powder-shaped rubbish derivatived fuel (RDF-4) and burns generation high-temperature flue gas through changing
Produce vapours after heat and carry out the garbage treating process of steam-electric power after actual motion after a while, find still to deposit
In some problems having been resolved possibly through technological improvement, such as: distributing rationally of crude waste resource cannot be accomplished；
Burn powder-shaped rubbish derivatived fuel (RDF-4) if the waste heat gas that the high-temperature flue gas produced produces after carrying out heat exchange absorption is directly arranged
Putting and can cause secondary pollution, if individual processing needs higher processing cost, heat energy cannot be fully used.
Summary of the invention
Waste resources is distributed rationally, heat energy makes full use of, extremely low two English discharges to it is an object of the invention to provide one
Biomass prepare RDF-4 smokeless burn steam-electric power technique.
The above-mentioned purpose of the present invention is realized by following technical proposal:
Biomass are prepared RDF-4 smokeless and are burned steam-electric power technique, including following step:
1) biomass are carried out broken bag process；
2) biomass after broken bag are carried out artificial screening；Select recyclable plastics, regeneration and granulation after cleaning；Select stone, brick
Blocks etc. crush, as environment-friendly building materials raw material after crushing；Select glass, clean laggard oozy glass wire drawing；
3) by step 2) residual refuse after artificial screening crosses tramp iron separator except ferrum；
4) will cross, except the rubbish after ferrum, No. 1 mechanical picker that aperture is 6cm；
5) siftage of in step 4) No. 1 mechanical picker is crossed No. 2 mechanical pickers that aperture is 2cm；
6) siftage of in step 5) No. 2 mechanical pickers is done compost treatment, form fertile soil；
7) oversize of in step 4) No. 1 mechanical picker is carried out coarse crushing, make the particle diameter of the material particles after crushing (except not having on a small quantity
Outside being crushed to) at below 6cm；
8) material after step 7) coarse crushing is crossed No. 3 mechanical pickers that aperture is 4cm；
9) oversize of in step 8) No. 3 mechanical pickers is carried out fine crushing, make the particle diameter of the material particles after crushing (except not having on a small quantity
Outside being crushed to) at below 4cm；
10) by No. 2 mechanical pickers in step 8) No. 3 siftage of mechanical picker, step 9) fine crushing gained material and step 5)
Hydraulic pressure dehydration is carried out after oversize mixing；
11) material completing hydraulic pressure dehydration is sent into biological drying room and carry out biological drying sterilization；
12) material after completing biological drying sterilization is sent in mechanical drying cylinder and is dried, and makes the material after drying contain
Water rate is less than 40%；
13) roll squeezer sent into by the material after drying, and makes powder-shaped rubbish derivatived fuel (RDF-4)；
14) powder-shaped rubbish derivatived fuel (RDF-4) feeding combustor is burned and collects the produced high-temperature flue gas of burning；
15) high-temperature flue gas is passed into waste heat boiler, after residual heat boiler for exchanging heat, produces vapours and discharge waste hot air body；
16) vapours is passed into steam turbine generator and carries out steam-electric power；
17) water produced by steam turbine generator during steam-electric power is passed into waste heat boiler as the water generating vapours
Source；
18) it is passed into step 15) is discharged waste heat gas in the mechanical drying cylinder of step 12) as drying heat source gas；
19) moisture that mechanical drying cylinder produces in drying course is condensed；
20) after being condensed by moisture, gained gas is passed in the combustor of step 14) in right amount, for the burning oxygen supply of its inside, with
Time also burn deodorization；
21) if moisture condensation after gained gas for step 20) after still have residue, enter this step: led to by remaining gas
Enter to the biological drying of step 11) indoor, increase heat energy for biological dry disinfection.
The invention has the beneficial effects as follows:
1, biomass are carried out classification and reclaim the raw material being respectively prepared plastic, glass and construction material, remain organic
Rubbish rolls makes powder-shaped rubbish derivatived fuel (RDF-4), it is achieved the comprehensive utilization of waste resource, plays maximum economic benefit；
2, burn powder-shaped rubbish derivatived fuel (RDF-4) and collect by burning produced high-temperature flue gas, utilizing heat-exchanger rig (remaining
Heat boiler) absorb the heat energy in high-temperature flue gas and produce vapours, utilize vapours to carry out steam-electric power, by residual heat boiler for exchanging heat
During the waste heat gas that produces for dried material rubbish, it is achieved recycling of heat energy, increase economic efficiency；
3, utilizing waste heat gas drying material rubbish, the flue dust in waste heat gas is played adsorption by material rubbish；A part
It is dried produced gas to be passed in biological drying room, increases the temperature that biological drying is indoor, improve biological drying sterilization
Efficiency；A part is dried produced gas and is passed in combustor, for powder-shaped rubbish derivatived fuel (RDF-4) burning oxygen supply
Remove foul smell simultaneously；Realize extremely low two English discharges, be substantially reduced the secondary pollution caused in garbage processing procedure.
Accompanying drawing explanation
Fig. 1 is present invention process flow chart.
Detailed description of the invention
Carry out technical scheme detailed further below by embodiment, but protection domain is not limited to this.
Embodiment: biomass are prepared RDF-4 smokeless and burned steam-electric power technique, as it is shown in figure 1, by collection
Biomass are through a series of process and roll and make powder-shaped rubbish derivatived fuel (RDF-4), and burn powder-shaped rubbish derivatived fuel
(RDF-4) and collect the produced high-temperature flue gas of burning, utilize high-temperature flue gas to pass through heat exchange to absorb and generate vapours, by vapours
It is passed into steam turbine generator and carries out steam-electric power.The waste heat gas produced during heat exchange absorbs is respectively used to drying garbage
Burn in oxygen supply with powder-shaped rubbish derivatived fuel (RDF-4), thus reach thermal source comprehensive utilization, extremely low two English discharges and increase
The purpose of economic benefit.Specifically include following step:
1) biomass (house refuse, garden waste, human and animal excreta and spoil etc. are referred to as biomass) collected are entered
Row broken bag processes, and abolishes refuse bag therein, makes rubbish shed and be convenient for next step process work；
2) biomass after broken bag are carried out artificial screening；Selecting recyclable plastics, regeneration and granulation after cleaning, as plastic shaping
Raw material；Select stone, fragment of brick etc. to crush, broken rear as the raw material making environment-friendly building materials；Select glass, clean laggard
Oozy glass wire drawing becomes the raw material of glass；
3) by step 2) residual refuse after artificial screening crosses tramp iron separator except ferrum；
4) will cross, except the rubbish after ferrum, No. 1 mechanical picker that aperture is 6cm；
5) siftage of in step 4) No. 1 mechanical picker is crossed No. 2 mechanical pickers that aperture is 2cm；
6) siftage of in step 5) No. 2 mechanical pickers is done compost treatment, form fertile soil；
7) oversize of in step 4) No. 1 mechanical picker is carried out coarse crushing, make the particle diameter of the material particles after crushing (except not having on a small quantity
Outside being crushed to) at below 6cm；
8) material after step 7) coarse crushing is crossed No. 3 mechanical pickers that aperture is 4cm；
9) oversize of in step 8) No. 3 mechanical pickers is carried out fine crushing, make the particle diameter of the material particles after crushing (except not having on a small quantity
Outside being crushed to) at below 4cm；
10) by No. 2 mechanical pickers in step 8) No. 3 siftage of mechanical picker, step 9) fine crushing gained material and step 5)
Hydraulic pressure dehydration is carried out after oversize mixing；
11) material completing hydraulic pressure dehydration is sent into biological drying room and (refer to another entitled " a kind of biological drying sterilization chamber "
Patent application) carry out biological drying sterilization；
12) material after completing biological drying sterilization is sent in mechanical drying cylinder and is dried, and makes the material after drying contain
Water rate is less than 40%；
Wherein, in step 10), it is every 40 ~ 60cm that hydraulic pressure is dehydrated its pressure size2Bear 400 ~ 600T pressure, make material aqueous
Rate (percentage by weight that moisture is overall with material) is less than 50%；In step 11), the material water ratio after biological drying sterilization is little
In 45%；This has concrete introduction in the patent application of another entitled " a kind of bioanalysis drying garbage sterilization process "；
13) roll squeezer sent into by the material after drying, and makes powder-shaped rubbish derivatived fuel (RDF-4)；
14) powder-shaped rubbish derivatived fuel (RDF-4) feeding combustor is burned and collects the produced high-temperature flue gas of burning；
15) high-temperature flue gas is passed into waste heat boiler, after residual heat boiler for exchanging heat, produces vapours and discharge waste hot air body；
16) vapours is passed into steam turbine generator and carries out steam-electric power；
17) water produced by steam turbine generator during steam-electric power is passed into waste heat boiler as the water generating vapours
Source；
18) it is passed into step 15) is discharged waste heat gas in the mechanical drying cylinder of step 12) as drying heat source gas；
19) carry out the moisture that mechanical drying cylinder produces in drying course condensing (condensed temperature is generally less than 50 °,
The moisture content making gas is down to 20% ~ 30%), to make water vapor condensation be aqueous water thus reduces gas gross, removes steam
Steam can also be avoided during next step oxygen supply to produce cooling effect；
20) after being condensed by moisture, gained gas is passed in the combustor of step 14) in right amount, for the burning oxygen supply of its inside, with
Time also burn deodorization；
21) if moisture condensation after gained gas for step 20) after still have residue, enter this step: led to by remaining gas
Enter to the biological drying of step 11) indoor, increase heat energy for biological dry disinfection, accelerate fermentation reaction, reduce fermentation dried
Time.
During June 2015 February in 2015, Fujian Zheng Ren environmental protection company limited utilizes the technical scheme in the present embodiment
Contrast experiment has been carried out with former technical scheme, found that: the biomass of isodose, utilize the technical scheme ratio in the present embodiment
Utilizing former technical scheme generated energy to improve more than 30%, dioxin emission is substantially reduced, and overall economic benefit improves more than 35%.
The foregoing is only the preferred embodiments of the present invention, be not limited to invention, although with reference to aforementioned enforcement
The present invention has been described in detail by example, and for a person skilled in the art, it still can be to foregoing embodiments
Described technical scheme is modified, or wherein portion of techniques feature is carried out equivalent.All invention spirit and
Within principle, any modification, equivalent substitution and improvement etc. made, within should be included in the protection domain of invention.
Claims (1)
1. biomass are prepared RDF-4 smokeless and are burned steam-electric power technique, it is characterised in that include following step:
1) biomass are carried out broken bag process；
2) biomass after broken bag are carried out artificial screening；Select recyclable plastics, regeneration and granulation after cleaning；Select stone, brick
Blocks etc. crush, as environment-friendly building materials raw material after crushing；Select glass, clean laggard oozy glass wire drawing；
3) by step 2) residual refuse after artificial screening crosses tramp iron separator except ferrum；
4) will cross, except the rubbish after ferrum, No. 1 mechanical picker that aperture is 6cm；
5) siftage of in step 4) No. 1 mechanical picker is crossed No. 2 mechanical pickers that aperture is 2cm；
6) siftage of in step 5) No. 2 mechanical pickers is done compost treatment, form fertile soil；
7) oversize of in step 4) No. 1 mechanical picker is carried out coarse crushing, make the particle diameter of the material particles after crushing (except not having on a small quantity
Outside being crushed to) at below 6cm；
8) material after step 7) coarse crushing is crossed No. 3 mechanical pickers that aperture is 4cm；
9) oversize of in step 8) No. 3 mechanical pickers is carried out fine crushing, make the particle diameter of the material particles after crushing (except not having on a small quantity
Outside being crushed to) at below 4cm；
10) by No. 2 mechanical pickers in step 8) No. 3 siftage of mechanical picker, step 9) fine crushing gained material and step 5)
Hydraulic pressure dehydration is carried out after oversize mixing；
11) material completing hydraulic pressure dehydration is sent into biological drying room and carry out biological drying sterilization；
12) material after completing biological drying sterilization is sent in mechanical drying cylinder and is dried, and makes the material after drying contain
Water rate is less than 40%；
13) roll squeezer sent into by the material after drying, and makes powder-shaped rubbish derivatived fuel (RDF-4)；
14) powder-shaped rubbish derivatived fuel (RDF-4) feeding combustor is burned and collects the produced high-temperature flue gas of burning；
15) high-temperature flue gas is passed into waste heat boiler, after residual heat boiler for exchanging heat, produces vapours and discharge waste hot air body；
16) vapours is passed into steam turbine generator and carries out steam-electric power；
17) water produced by steam turbine generator during steam-electric power is passed into waste heat boiler as the water generating vapours
Source；
18) it is passed into step 15) is discharged waste heat gas in the mechanical drying cylinder of step 12) as drying heat source gas；
19) moisture that mechanical drying cylinder produces in drying course is condensed；
20) after being condensed by moisture, gained gas is passed in the combustor of step 14), in right amount for the burning oxygen supply of its inside；
21) if moisture condensation after gained gas for step 20) after still have residue, enter this step: led to by remaining gas
Enter to the biological drying of step 11) indoor, increase heat energy for biological dry disinfection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610488760.0A CN106111667A (en) | 2016-06-29 | 2016-06-29 | Biomass are prepared RDF 4 smokeless and are burned steam-electric power technique |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610488760.0A CN106111667A (en) | 2016-06-29 | 2016-06-29 | Biomass are prepared RDF 4 smokeless and are burned steam-electric power technique |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106111667A true CN106111667A (en) | 2016-11-16 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610488760.0A Pending CN106111667A (en) | 2016-06-29 | 2016-06-29 | Biomass are prepared RDF 4 smokeless and are burned steam-electric power technique |
Country Status (1)
| Country | Link |
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| CN (1) | CN106111667A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106734061A (en) * | 2016-11-28 | 2017-05-31 | 中国环境科学研究院 | Rubbish combined treatment process and system |
| CN110805914A (en) * | 2019-11-11 | 2020-02-18 | 江苏华旭环保股份有限公司 | Rotary kiln drying incineration process for PTA activated sludge with additional pre-dryer |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2010202689A (en) * | 2009-02-27 | 2010-09-16 | Bio Coke Lab Co Ltd | Gasification method, power generation method, gasification device, power generation device, and organic material |
| CN201836894U (en) * | 2010-10-22 | 2011-05-18 | 河南省澳斯迪环保机械有限责任公司 | Garbage incinerator |
| CN103934251A (en) * | 2014-01-21 | 2014-07-23 | 上海程胜环保科技有限公司 | Human household garbage disposition and recycling method |
| CN105443171A (en) * | 2014-08-20 | 2016-03-30 | 福建正仁环保有限公司 | Incineration power generation process adopting refuse derived fuel (RDF) prepared from refuse |
-
2016
- 2016-06-29 CN CN201610488760.0A patent/CN106111667A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2010202689A (en) * | 2009-02-27 | 2010-09-16 | Bio Coke Lab Co Ltd | Gasification method, power generation method, gasification device, power generation device, and organic material |
| CN201836894U (en) * | 2010-10-22 | 2011-05-18 | 河南省澳斯迪环保机械有限责任公司 | Garbage incinerator |
| CN103934251A (en) * | 2014-01-21 | 2014-07-23 | 上海程胜环保科技有限公司 | Human household garbage disposition and recycling method |
| CN105443171A (en) * | 2014-08-20 | 2016-03-30 | 福建正仁环保有限公司 | Incineration power generation process adopting refuse derived fuel (RDF) prepared from refuse |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106734061A (en) * | 2016-11-28 | 2017-05-31 | 中国环境科学研究院 | Rubbish combined treatment process and system |
| CN110805914A (en) * | 2019-11-11 | 2020-02-18 | 江苏华旭环保股份有限公司 | Rotary kiln drying incineration process for PTA activated sludge with additional pre-dryer |
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Application publication date: 20161116 |
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