CN209068514U - Refuse gasification dual firing chamber flue gas Boiler Steam screw expansion electricity generation system - Google Patents
Refuse gasification dual firing chamber flue gas Boiler Steam screw expansion electricity generation system Download PDFInfo
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- CN209068514U CN209068514U CN201821565374.8U CN201821565374U CN209068514U CN 209068514 U CN209068514 U CN 209068514U CN 201821565374 U CN201821565374 U CN 201821565374U CN 209068514 U CN209068514 U CN 209068514U
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- Prior art keywords
- flue gas
- air
- gas boiler
- air blower
- gasification
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- 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.)
- Expired - Fee Related
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- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 79
- 239000003546 flue gas Substances 0.000 title claims abstract description 78
- 238000002309 gasification Methods 0.000 title claims abstract description 47
- 230000005611 electricity Effects 0.000 title claims abstract description 13
- 238000010304 firing Methods 0.000 title claims abstract description 11
- 230000009977 dual effect Effects 0.000 title claims abstract description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 40
- 239000007789 gas Substances 0.000 claims abstract description 34
- 238000002485 combustion reaction Methods 0.000 claims abstract description 31
- 239000002737 fuel gas Substances 0.000 claims abstract description 20
- 239000010813 municipal solid waste Substances 0.000 claims abstract description 19
- 239000000446 fuel Substances 0.000 claims abstract description 13
- 239000003517 fume Substances 0.000 claims abstract description 6
- 239000000779 smoke Substances 0.000 claims description 25
- 230000001939 inductive effect Effects 0.000 claims description 7
- 239000002253 acid Substances 0.000 claims description 5
- 229910052799 carbon Inorganic materials 0.000 claims description 5
- 239000003610 charcoal Substances 0.000 claims description 5
- 238000010248 power generation Methods 0.000 claims description 5
- 239000002250 absorbent Substances 0.000 claims description 3
- 230000002745 absorbent Effects 0.000 claims description 3
- 239000002918 waste heat Substances 0.000 claims description 2
- 230000008676 import Effects 0.000 claims 1
- 239000003344 environmental pollutant Substances 0.000 abstract description 7
- 231100000719 pollutant Toxicity 0.000 abstract description 7
- 238000000354 decomposition reaction Methods 0.000 abstract description 2
- 239000002699 waste material Substances 0.000 abstract description 2
- 238000001914 filtration Methods 0.000 description 10
- 238000000034 method Methods 0.000 description 9
- 239000000428 dust Substances 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 235000019504 cigarettes Nutrition 0.000 description 5
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- 238000004064 recycling Methods 0.000 description 4
- 239000002910 solid waste Substances 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000003595 mist Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 150000003384 small molecules Chemical class 0.000 description 2
- 206010002660 Anoxia Diseases 0.000 description 1
- 241000976983 Anoxia Species 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- 230000007953 anoxia Effects 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000009264 composting Methods 0.000 description 1
- 239000000039 congener Substances 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- 239000000383 hazardous chemical Substances 0.000 description 1
- 239000011344 liquid material Substances 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000000505 pernicious effect Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Gasification And Melting Of Waste (AREA)
- Processing Of Solid Wastes (AREA)
- Treating Waste Gases (AREA)
Abstract
The utility model discloses refuse gasification dual firing chamber flue gas Boiler Steam screw expansion electricity generation systems, are related to technical field of waste treatment.The utility model includes belt conveyor, screw conveyor, gasification furnace, air blower, second-time burning air blower, secondary combustion chamber, flue gas boiler, main steam header, screw expansion generating set, extracting tower, activated charcoal adding apparatus, bag filter, air-introduced machine and chimney;Granulated garbage fuel is transported in the feed hopper of screw conveyor by belt conveyor.The utility model realizes that gasification decomposition generates the fuel gas of certain temperature by the gasification furnace and air blower of design, fuel gas is adequately burnt while improving the temperature of fuel gas by second-time burning air blower and secondary combustion chamber, improve efficiency of combustion, the pollutant in multistage removal flue gas is carried out by extracting tower, activated charcoal adding apparatus and bag filter, solves the problems, such as that existing combustion product gases temperature is low and fume treatment is incomplete.
Description
Technical field
The utility model belongs to technical field of waste treatment, more particularly to refuse gasification dual firing chamber flue gas Boiler Steam spiral shell
Bar expansion power generation system.
Background technique
The gasification of house refuse is a kind of novel technology of garbage disposal, compared with burning, landfill and composting treatment method,
Gasification Technique is increasingly valued by people because having many advantages, such as clean and environmental protection, resource recycling.People make every effort to
House refuse is handled with gasification technology, to reach more preferably innoxious, minimizing, recycling effect.In refuse gasification reactor
In, organic matter heats under anaerobic or anoxia condition, and the chemical combination key of organic compound is broken, and is converted to by macromolecule small
The combustion gas of molecular weight, oil or grease liquid material and coke etc..
Existing rubbish vaporescence mostly uses the closed environment of no gas supply, the temperature of decomposition of gasifying 500 DEG C-
700 DEG C, the initial temperature of fuel gas is lower in entering secondary combustion chamber, and oxygen content is lower, second-time burning process reaction
Not exclusively, flue-gas temperature is lower after burning, and efficiency of combustion is low, and the flue gas of generation is carried out solid gas point mostly by existing incineration firing
It is then discharged from after by washing, a variety of hazardous materials effectively can not be subjected to classification processing, caused in the gas of release still
So there are a large amount of small pollution particles.
Summary of the invention
The purpose of this utility model is to provide refuse gasification dual firing chamber flue gas Boiler Steam screw expansion electricity generation systems, lead to
The gasification furnace and air blower for crossing design realize that the fuel gas for generating certain temperature, second-time burning air blower and secondary are decomposed in gasification
Fuel gas is adequately burnt while improving the temperature of fuel gas by combustion chamber, is improved efficiency of combustion, is passed through extracting tower, activity
Charcoal throwing device and bag filter carry out the pollutant in multistage removal flue gas, solve that existing combustion product gases temperature is low and cigarette
The incomplete problem of gas disposal.
In order to solve the above technical problems, the utility model is achieved through the following technical solutions:
The utility model is refuse gasification dual firing chamber flue gas Boiler Steam screw expansion electricity generation system, including Belt Conveying
Machine, screw conveyor, gasification furnace, air blower, second-time burning air blower, secondary combustion chamber, flue gas boiler, main steam header, screw rod
Expansion power generation unit, extracting tower, activated charcoal adding apparatus, bag filter, air-introduced machine and chimney;The belt conveyor is by rubbish
Rubbish granular fuel is transported in the feed hopper of screw conveyor;The screw conveyor is quantitative to be transported to gas for granulated garbage fuel
Change the feed inlet of furnace;The fuel gas outlet of the gasification furnace passes through gas pipeline and secondary combustion chamber fuel gas entrance phase
Even;The blower outlet is connected by the first air inducing pipeline with gasification furnace air inlet;The second-time burning air blower passes through
Second air inducing pipeline is connected with secondary combustion chamber air inlet;Secondary combustion chamber hot fume outlet and flue gas boiler hot flue gas into
Mouth is connected;The flue gas boiler high temperature higher pressure steam outlet passes through main steam header and screw expansion generating set steam inlet phase
Even;The flue gas boiler afterheat flue gas is connected by the first smoke tube with extracting tower smoke air inlet;The depickling tower flue gas
Gas outlet is connected by the second smoke tube with bag filter air inlet;The bag filter gas outlet passes through third flue gas
Conduit is connected with fan inlet;The fan out draft passes through the air inlet phase of the 4th smoke tube and chimney bottom
Even;The air that granulated garbage fuel and air blower blast in the gasification furnace generates flammable in closed space high temperature burning
Gas;The imflammable gas includes carbon monoxide, hydrogen and methane;It is roused in the secondary combustion chamber with second-time burning air blower
The air entered is mixed, and second-time burning further increases that flue-gas temperature is higher, and flue-gas temperature reaches under original gasification temperature
To 1100 DEG C or more;The flue gas boiler, main steam header and screw expansion generating set are connected, and flue gas boiler is by 1100 DEG C
Flue gas heat exchange after generate high temperature and pressure steam, conveyed by main steam header, screw expansion generating set is in high temperature height
It generates electricity under the action of pressure steam;The extracting tower is by way of the wet type deacidification of solid waste flue gas to the flue gas after energy exchange
The filtering of carry out solid waste and dissolution harmful smoke;The bag filter carries out again the minute dusts not filtered in flue gas
Secondary filtering, flue gas after filtering can reach discharge standard;The air-introduced machine increases the gas that can be discharged after filtering
Pass through smoke stack emission to eminence after pressure;The activated charcoal adding apparatus is arranged on the second smoke tube, to taking out of in extracting tower
The nuisances such as acid mist carry out absorption and reduce pollutant concentration, reduce acid mist etc. in bag filter filter process to equipment corruption
Erosion.
Further, electricity-generating method the following steps are included:
SS001 gasification is decomposed, and the granulated garbage fuel and air blower for the addition being transported in gasification furnace are always supplied to gasification furnace
Under conditions of gas, gasification temperature reaches 710 DEG C -840 DEG C, and granulated garbage fuel carries out pyrolytic gasification reaction, and big point in rubbish
Sub- steady state mass resolves into the inflammable fuel gas of small molecule;
The fuel gas generated in SS001 is input to by gas pipeline defeated in secondary combustion chamber by SS002 second-time burning
The fuel gas entered and the air that second-time burning air blower blasts mix full combustion, flue-gas temperature reach 1100 DEG C with
On;
The high-temperature flue gas generated in SS002 is passed through and carries out returning for thermal energy in flue gas boiler by the recycling of SS003 flue gas heat
It receives, heats the water vapour that the water in flue gas boiler generates high temperature and pressure;
The water vapour of the high temperature and pressure generated in SS003 is conveyed to screw expansion hair by main steam header by SS004 power generation
Motor group generates electricity, and screw expansion generating set is grid-connected with power grid;
The low energy flue gas after the recovery of thermal energy in SS003 is transported in extracting tower and carries out at depickling by SS005 deacidifying flue gas
Reason, further decreases flue-gas temperature;
Flue gas in SS005 by cooling depickling is passed through bag-type dust by the second smoke tube by SS006 flue gas ash removal
Bag-type dust is carried out in device, the activated charcoal adding apparatus on the second smoke tube is interrupted continuous addition into the second smoke tube and lives
Property charcoal the harmful substance in flue gas is adsorbed, reduce gas pollutant content, reach discharge standard;
SS007 flue gas emission is pressurized the gas after dust removal and filtration in SS006 by air-introduced machine, is transported to chimney
Middle carry out high altitude discharge.
Further, active carbon includes powdered activated carbon or block absorbent charcoal in the activated charcoal adding apparatus.
The utility model has the following beneficial effects:
1, the utility model improves the temperature that gasification is decomposed by the gasification furnace and air blower of design and improves combustible gas simultaneously
The initial temperature of body, second-time burning air blower and secondary combustion chamber adequately burn fuel gas, and flue-gas temperature reaches 1100
DEG C or more improve efficiency of combustion, improve the economic benefit of garbage power.
2, the utility model is carried out in classification removal flue gas not by extracting tower, activated charcoal adding apparatus and bag filter
Congener pollutant reduces microminiature pollution by adding the small harmful suspension of activated carbon adsorption and pernicious gas molecule
The content of object achievees the effect that environmental protection.
Certainly, any product for implementing the utility model does not necessarily require achieving all the advantages described above at the same time.
Detailed description of the invention
In order to illustrate more clearly of the technical solution of the utility model embodiment, make required for being described below to embodiment
Attached drawing is briefly described, it should be apparent that, the drawings in the following description are merely some embodiments of the present invention,
For those of ordinary skill in the art, without creative efforts, it can also be obtained according to these attached drawings
Other attached drawings.
Fig. 1 is that the process of the utility model refuse gasification dual firing chamber flue gas Boiler Steam screw expansion electricity generation system is illustrated
Figure;
In attached drawing, parts list represented by the reference numerals are as follows:
1- belt conveyor, 2- screw conveyor, 3- gasification furnace, 4- air blower, 5- second-time burning air blower, 6- bis- times combustions
Burn room, 7- flue gas boiler, 8- main steam header, 9- screw expansion generating set, 10- extracting tower, 11- activated charcoal adding apparatus, 12-
Bag filter, 13- air-introduced machine, 14- chimney.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without creative efforts
All other embodiment obtained, fall within the protection scope of the utility model.
Refering to Figure 1, the utility model is refuse gasification dual firing chamber flue gas Boiler Steam screw expansion electricity generation system,
Including belt conveyor 1, screw conveyor 2, gasification furnace 3, air blower 4, second-time burning air blower 5, secondary combustion chamber 6, flue gas
Boiler 7, main steam header 8, screw expansion generating set 9, extracting tower 10, activated charcoal adding apparatus 11, bag filter 12, air inducing
Machine 13 and chimney 14;
Granulated garbage fuel is transported in the feed hopper of screw conveyor 2 by belt conveyor 1;Screw conveyor 2 is quantitative
Granulated garbage fuel is transported to the feed inlet of gasification furnace 3;The fuel gas outlet of gasification furnace 3 passes through gas pipeline and secondary combustion
6 fuel gas entrance of room is burnt to be connected;
4 air outlet of air blower is connected by the first air inducing pipeline with 3 air inlet of gasification furnace;Second-time burning air blower 5 passes through
Second air inducing pipeline is connected with 6 air inlet of secondary combustion chamber;6 hot fume of secondary combustion chamber outlet with 7 hot fume of flue gas boiler into
Mouth is connected;The outlet of 7 high temperature and high pressure steam of flue gas boiler is connected by main steam header 8 with 9 steam inlet of screw expansion generating set;
7 waste heat flue gas of flue gas boiler is connected by the first smoke tube with 10 smoke air inlet of extracting tower;10 cigarette of extracting tower
Gas gas outlet is connected by the second smoke tube with 12 air inlet of bag filter;12 gas outlet of bag filter passes through third cigarette
Airway is connected with 13 air inlet of air-introduced machine;13 air outlet of air-introduced machine passes through the air inlet of the 4th smoke tube and 14 bottom of chimney
It is connected;
The air that granulated garbage fuel and air blower 4 blast in gasification furnace 3 is generated in closed space high temperature burning can
Combustion property gas;Imflammable gas includes carbon monoxide, hydrogen and methane;
The air blasted in secondary combustion chamber 6 with second-time burning air blower 5 is mixed, and second-time burning is in original gasification
At a temperature of further increase that flue-gas temperature is higher, and flue-gas temperature reaches 1100 DEG C or more;
Flue gas boiler 7, main steam header 8 and screw expansion generating set 9 are connected, and flue gas boiler 7 is by 1100 DEG C of cigarette
The steam that high temperature and pressure is generated after gas heat exchange, is conveyed, screw expansion generating set 9 is in high temperature and pressure by main steam header 8
It generates electricity under the action of steam;
Extracting tower 10 solid waste flue gas by way of wet type deacidification to the flue gas after energy exchange carry out solid waste filtering with
And dissolution harmful smoke;
Bag filter 12 is for re-filtering to the minute dusts not filtered in flue gas, flue gas after filtering
Reach discharge standard;
Air-introduced machine 13 passes through chimney 14 after being pressurized the gas that can be discharged after filtering and is discharged into eminence;Active carbon is thrown
Feeder apparatus 11 is arranged on the second smoke tube, and carrying out absorption to nuisances such as the acid mists taken out of in extracting tower 10 reduces pollutant
Concentration reduces acid mist etc. and corrodes in 12 filter process of bag filter to equipment.
Wherein, electricity-generating method the following steps are included:
SS001 gasification is decomposed, and granulated garbage fuel and the air blower 4 for being transported to the addition in gasification furnace 3 are total to gasification furnace 3
Under conditions of gas supply, gasification temperature reaches 710 DEG C -840 DEG C, and granulated garbage fuel carries out pyrolytic gasification reaction, big in rubbish
Molecule steady state mass resolves into the inflammable fuel gas of small molecule;
The fuel gas generated in SS001 is input in secondary combustion chamber 6 by SS002 second-time burning by gas pipeline
The fuel gas of input carries out mixing full combustion with the air that second-time burning air blower 5 blasts, and flue-gas temperature reaches 1100 DEG C
More than;
The high-temperature flue gas generated in SS002 is passed through and carries out returning for thermal energy in flue gas boiler 7 by the recycling of SS003 flue gas heat
It receives, heats the water vapour that the water in flue gas boiler 7 generates high temperature and pressure;
The water vapour of the high temperature and pressure generated in SS003 is conveyed to screw expansion by main steam header 8 by SS004 power generation
Generating set 9 generates electricity, and screw expansion generating set 9 and power grid are grid-connected;
The low energy flue gas after the recovery of thermal energy in SS003 is transported in extracting tower 10 and carries out at depickling by SS005 deacidifying flue gas
Reason, further decreases flue-gas temperature;
Flue gas in SS005 by cooling depickling is passed through bag-type dust by the second smoke tube by SS006 flue gas ash removal
Bag-type dust is carried out in device 12, the activated charcoal adding apparatus 11 on the second smoke tube is interrupted into the second smoke tube continuously to be added
Add active carbon to adsorb the harmful substance in flue gas, reduces gas pollutant content, reach discharge standard;
SS007 flue gas emission is pressurized the gas after dust removal and filtration in SS006 by air-introduced machine 13, is transported to cigarette
High altitude discharge is carried out in chimney 14.
Wherein, active carbon includes powdered activated carbon or block absorbent charcoal in activated charcoal adding apparatus 11.
In the description of this specification, the description of reference term " one embodiment ", " example ", " specific example " etc. means
Particular features, structures, materials, or characteristics described in conjunction with this embodiment or example are contained at least one of the utility model
In embodiment or example.In the present specification, schematic expression of the above terms be not necessarily referring to identical embodiment or
Example.Moreover, particular features, structures, materials, or characteristics described can be in any one or more embodiment or examples
In can be combined in any suitable manner.
The preferred embodiment in the utility model disclosed above is only intended to help to illustrate the utility model.Preferred embodiment is simultaneously
There is no the details that detailed descriptionthe is all, also not limiting the utility model is only the specific embodiment.Obviously, according to this theory
The content of bright book can make many modifications and variations.These embodiments are chosen and specifically described to this specification, is in order to preferably
The principles of the present invention and practical application are explained, so that skilled artisan be enable to better understand and utilize this
Utility model.The utility model is limited only by the claims and their full scope and equivalents.
Claims (2)
1. refuse gasification dual firing chamber flue gas Boiler Steam screw expansion electricity generation system, including belt conveyor (1), screw conveyor
(2), gasification furnace (3), air blower (4), second-time burning air blower (5), secondary combustion chamber (6), flue gas boiler (7), main steam header
(8), screw expansion generating set (9), extracting tower (10), activated charcoal adding apparatus (11), bag filter (12), air-introduced machine
(13) and chimney (14), it is characterised in that:
Granulated garbage fuel is transported in the feed hopper of screw conveyor (2) by the belt conveyor (1);The helical feed
The quantitative feed inlet that granulated garbage fuel is transported to gasification furnace (3) of machine (2);The fuel gas outlet of the gasification furnace (3) is logical
Gas pipeline is crossed to be connected with secondary combustion chamber (6) fuel gas entrance;
Air blower (4) air outlet is connected by the first air inducing pipeline with gasification furnace (3) air inlet;The second-time burning air blast
Machine (5) is connected by the second air inducing pipeline with secondary combustion chamber (6) air inlet;Secondary combustion chamber (6) hot fume outlet with
Flue gas boiler (7) hot fume import is connected;Main steam header (8) and spiral shell are passed through in flue gas boiler (7) the high temperature and high pressure steam outlet
Bar expansion power generation unit (9) steam inlet is connected;
Flue gas boiler (7) the waste heat flue gas is connected by the first smoke tube with extracting tower (10) smoke air inlet;It is described de-
Acid tower (10) flue gas gas outlet is connected by the second smoke tube with bag filter (12) air inlet;The bag filter
(12) gas outlet is connected by third smoke tube with air-introduced machine (13) air inlet;Air-introduced machine (13) air outlet passes through the 4th
Smoke tube is connected with the air inlet of chimney (14) bottom;The activated charcoal adding apparatus (11) is arranged in the second smoke tube
On.
2. refuse gasification dual firing chamber flue gas Boiler Steam screw expansion electricity generation system according to claim 1, feature exist
In active carbon includes powdered activated carbon or block absorbent charcoal in the activated charcoal adding apparatus (11).
Priority Applications (1)
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CN201821565374.8U CN209068514U (en) | 2018-09-25 | 2018-09-25 | Refuse gasification dual firing chamber flue gas Boiler Steam screw expansion electricity generation system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201821565374.8U CN209068514U (en) | 2018-09-25 | 2018-09-25 | Refuse gasification dual firing chamber flue gas Boiler Steam screw expansion electricity generation system |
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Publication Number | Publication Date |
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CN209068514U true CN209068514U (en) | 2019-07-05 |
Family
ID=67093253
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CN201821565374.8U Expired - Fee Related CN209068514U (en) | 2018-09-25 | 2018-09-25 | Refuse gasification dual firing chamber flue gas Boiler Steam screw expansion electricity generation system |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109268836A (en) * | 2018-09-25 | 2019-01-25 | 无锡市特能机电有限公司 | Refuse gasification dual firing chamber flue gas Boiler Steam screw expansion electricity generation system |
CN111288452A (en) * | 2020-02-12 | 2020-06-16 | 王丽枝 | Conveying system for pyrolysis and gasification of garbage |
CN111288461A (en) * | 2020-04-10 | 2020-06-16 | 上海东石塘再生能源有限公司 | Control system and method for controlling charging amount of sludge |
CN113685823A (en) * | 2021-08-20 | 2021-11-23 | 乾健天勤环保设备(江苏)有限公司 | Vertical incinerator system and process flow |
-
2018
- 2018-09-25 CN CN201821565374.8U patent/CN209068514U/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109268836A (en) * | 2018-09-25 | 2019-01-25 | 无锡市特能机电有限公司 | Refuse gasification dual firing chamber flue gas Boiler Steam screw expansion electricity generation system |
CN111288452A (en) * | 2020-02-12 | 2020-06-16 | 王丽枝 | Conveying system for pyrolysis and gasification of garbage |
CN111288461A (en) * | 2020-04-10 | 2020-06-16 | 上海东石塘再生能源有限公司 | Control system and method for controlling charging amount of sludge |
CN113685823A (en) * | 2021-08-20 | 2021-11-23 | 乾健天勤环保设备(江苏)有限公司 | Vertical incinerator system and process flow |
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Granted publication date: 20190705 |