CN108518255A - A kind of 500KW mobile containers biomass power generation system - Google Patents
A kind of 500KW mobile containers biomass power generation system Download PDFInfo
- Publication number
- CN108518255A CN108518255A CN201810506482.6A CN201810506482A CN108518255A CN 108518255 A CN108518255 A CN 108518255A CN 201810506482 A CN201810506482 A CN 201810506482A CN 108518255 A CN108518255 A CN 108518255A
- Authority
- CN
- China
- Prior art keywords
- boiler
- container system
- steam turbine
- burner
- charger
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000002028 Biomass Substances 0.000 title claims abstract description 20
- 238000010248 power generation Methods 0.000 title claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 31
- 238000004064 recycling Methods 0.000 claims abstract description 11
- 239000000446 fuel Substances 0.000 claims abstract description 7
- 239000002828 fuel tank Substances 0.000 claims abstract description 5
- 239000002002 slurry Substances 0.000 claims description 10
- 238000005507 spraying Methods 0.000 claims description 8
- 239000007921 spray Substances 0.000 claims description 6
- 239000003245 coal Substances 0.000 abstract description 5
- 238000003915 air pollution Methods 0.000 abstract description 2
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 239000004071 soot Substances 0.000 abstract description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 12
- 239000003546 flue gas Substances 0.000 description 12
- 239000007789 gas Substances 0.000 description 6
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- 230000002745 absorbent Effects 0.000 description 4
- 239000002250 absorbent Substances 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical group [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 238000006477 desulfuration reaction Methods 0.000 description 2
- 230000023556 desulfurization Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 230000029553 photosynthesis Effects 0.000 description 2
- 238000010672 photosynthesis Methods 0.000 description 2
- 230000009257 reactivity Effects 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 239000004484 Briquette Substances 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000004177 carbon cycle Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 1
- 229910010271 silicon carbide Inorganic materials 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- SUKJFIGYRHOWBL-UHFFFAOYSA-N sodium hypochlorite Chemical compound [Na+].Cl[O-] SUKJFIGYRHOWBL-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- 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
- F01K27/00—Plants for converting heat or fluid energy into mechanical energy, not otherwise provided for
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/48—Sulfur compounds
- B01D53/50—Sulfur oxides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/54—Nitrogen compounds
- B01D53/56—Nitrogen oxides
-
- 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
- F01K21/00—Steam engine plants not otherwise provided for
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B33/00—Steam-generation plants, e.g. comprising steam boilers of different types in mutual association
- F22B33/12—Self-contained steam boilers, i.e. comprising as a unit the steam boiler, the combustion apparatus, the fuel storage, accessory machines and equipment
Abstract
The invention discloses a kind of 500KW mobile containers biomass power generation systems, including boiler container system, boiler auxiliaries container system and steam turbine and its ancillary equipment container system, boiler container system includes charger, burner, boiler, divide drum and recycling pond, charger is located at one end in boiler container, the discharge port end of charger connects burner, the outlet end of burner connects boiler, a certain amount of demineralized water is housed in boiler, and the steam drain end of boiler is fixed and is communicated with a point drum, the steam turbine for dividing the venthole of drum to fix connection steam turbine and its ancillary equipment container system, steam turbine and its ancillary equipment container system include generator, steam turbine, fuel tank, condenser, condensate pump and water circulating pump.The energy consumption of this system is mainly stalk resource, is to make full use of biomass fuel, less power plant soot consumption；Air pollution is reduced, coal resources are saved.
Description
Technical field
The present invention relates to biomass generation field, specially a kind of 500KW mobile containers biomass power generation system
System.
Background technology
Biomass is that tellurian solar energy is utilized in photosynthesis of plant, and the biomass generated every year through photosynthesis is about
1700 × 108t, energy is approximately equivalent to 10 times of current world fuel consumption, and the utilization as the energy is less than it always
The 1% of amount.These biomass not being used, to complete the carbon cycle of nature, the overwhelming majority will by natural decomposition
Amount and carbon release, return in nature.On the other hand, due to the exhaustive exploitation of fossil energy and consumption, cause global
Energy crisis and environmental pollution, the fossil fuels increasingly depleted such as coal, oil, natural gas, therefore tap a new source of energy and seem particularly heavy
It wants.
China's biomass resource is abundant, but major part does not add utilization, the implementation of this engineering to be preciousness by these resource conversions
Electric power, open up the frontier of renewable energy utilization, fully realize turning waste into wealth and comprehensively utilizing for resource.Year uses biology
Matter fuel 5600t converts into standard coal 2800t, primary energy has been saved, thus it is proposed that a kind of 500KW mobile containers
Biomass power generation system is for solving the above problems.
Invention content
The purpose of the present invention is to provide a kind of 500KW mobile containers biomass power generation systems, to solve the above-mentioned back of the body
The problem of being proposed in scape technology.
To achieve the above object, the present invention provides the following technical solutions：A kind of 500KW mobile containers biomass power generation
System, including boiler container system, boiler auxiliaries container system and steam turbine and its ancillary equipment container system,
The boiler container system includes charger, burner, boiler, drum and recycling pond, the charger is divided to be located at boiler
The discharge port end of one end in container, the charger connects burner, and the outlet end of the burner connects boiler, the pot
A certain amount of demineralized water is housed, and the steam drain end of boiler is fixed and is communicated with a point drum in stove, the venthole for dividing drum is solid
Surely the steam turbine of steam turbine and its ancillary equipment container system, the steam turbine and its ancillary equipment container system packet are connected to
Generator, steam turbine, fuel tank, condenser, condensate pump and water circulating pump are included, the drive shaft end of the steam turbine is fixedly connected with hair
Motor, and the steam output end of steam turbine fixes connection condenser by pipeline, the hot well of the condenser is drawn through a manifold, point
Two-way to two condensate pump entrances, two condensate pumps are connected to recycling pond by pipeline, and the recycling pond passes through
Water circulating pump is connected to boiler, and the exhanst gas outlet of the burner connects province's coal of boiler auxiliaries container system by pipeline
The outlet port of device, the economizer is connected to bag filter, and compressed air reservoir is communicated in the bag filter, described
Compressed air reservoir is equipped with air compressor, and the outlet side of bag filter is connected to desulfuring and denitrifying apparatus by air-introduced machine,
The desulfuring and denitrifying apparatus is equipped with chimney, and one end of the boiler auxiliaries container system is fixed with water tank, described
Water tank is connected to Full-automatic water treatment device, and the Full-automatic water treatment device is connected to the end to intake on economizer by feed pump,
The water inlet end of the economizer upper water-out mouth end connection boiler.
The charger fuel is biomass block, and grain size is no more than 10mm.
Three layers of spraying layer are equipped in the desulfuring and denitrifying apparatus, and desulfuring and denitrifying apparatus bottom end is communicated with slurries pump, it is described
Using the nozzle of round inlet zone in spraying layer, hydrojet is conical hollow shape, and spray angle is 60-120 °.
Compared with prior art, the beneficial effects of the invention are as follows：
1, the energy consumption of this system is mainly stalk resource, is to make full use of biomass fuel, less power plant soot disappears
Consumption；Air pollution is reduced, coal resources are saved；
2, air is sent into burner by primary air fan and overfire air fan, and stalk briquette fuel is supported to burn in burner,
The flame and high-temperature flue gas that burning generates enter Boiler radiation area, convective region subsequently into economizer, generate low-temperature dust-containing flue gas
Into bag filter, sulfur-bearing, oxynitrides flue gas be sent into desulphurization denitration flue gas purifying equipment through air-introduced machine, under this equipment
If three layers of spray equipment, reach desulfurization off sulfide effect, gas slowly rises again by after demister demisting, meet the requirement of environmental protection is clean
Neat stress is discharged into through chimney in air.
3, the control and monitoring of Turbo-generator Set are completed by being arranged in the centralized control room operator station of container, with
Display and keyboard and mouse are the main monitoring of unit and control means, and operations staff can be in a small amount of local operation and touring inspection
It looks into and realizes Unit Commitment function under cooperation in centralized control room, the operating condition of unit is monitored and adjusted.
Description of the drawings
Fig. 1 is schematic structural view of the invention；
Fig. 2 is boiler container system structural schematic diagram of the present invention；
Fig. 3 is boiler auxiliaries container system structural schematic diagram of the present invention；
Fig. 4 is steam turbine of the present invention and its ancillary equipment container system structural schematic diagram.
In figure：Boiler container system 1, burner 12, boiler 13, divides drum 14, recycling pond 15, pot at charger 11
Stove ancillary equipment container system 2, water tank 21, Full-automatic water treatment device 22, feed pump 23, economizer 24, compressed air storage
Tank 25, air compressor 26, bag filter 27, air-introduced machine 28, desulfuring and denitrifying apparatus 29, chimney 210, slurries pump 211, steamer
Machine and its ancillary equipment container system 3, generator 31, steam turbine 32, fuel tank 33, condenser 34, condensate pump 35, recirculated water
Pump 36
Specific implementation mode
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation describes, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other
Embodiment shall fall within the protection scope of the present invention.
- 3 are please referred to Fig.1, the present invention provides a kind of technical solution：A kind of 500KW mobile containers biomass power generation system
System, including boiler container system 1, boiler auxiliaries container system 2 and steam turbine and its ancillary equipment container system
3, the boiler container system 1 include charger 11, burner 12, boiler 13, divide drum 14 and recycling pond 15, it is described into
Material machine 11 is located at one end in boiler container, and the discharge port end of the charger 11 connects burner 12, the burner 12
Outlet end connects boiler 13, a certain amount of demineralized water is housed, and the steam drain end of boiler 13 is fixed and is communicated in the boiler 13
Drum 14, the venthole for dividing drum 14 is divided to fix the steam turbine 32 for being connected to steam turbine and its ancillary equipment container system 3,
The steam turbine and its ancillary equipment container system 3 include generator 31, steam turbine 32, fuel tank 33, condenser 34, condensed water
The drive shaft end of pump 35 and water circulating pump 36, the steam turbine 32 is fixedly connected with generator 31, and the steam output end of steam turbine 32 is logical
Piping fixes connection condenser 34, and the hot well of the condenser 34 is drawn through a manifold, is divided to two-way to two condensate pumps
35 entrances, two condensate pumps 35 are connected to recycling pond 15 by pipeline, and the recycling pond 15 passes through water circulating pump 36
It is connected to boiler 13, the exhanst gas outlet of the burner 12 connects the economizer of boiler auxiliaries container system 2 by pipeline
24, the outlet port of the economizer 24 is connected to bag filter 27, and compressed air storage is communicated in the bag filter 27
Tank 25, the compressed air reservoir 25 is equipped with air compressor 26, and the outlet side of bag filter 27 passes through air-introduced machine 28
It is connected to desulfuring and denitrifying apparatus 29, the desulfuring and denitrifying apparatus 29 is equipped with chimney 210, the boiler auxiliaries container system
2 one end is fixed with water tank 21, and the water tank 21 is connected to Full-automatic water treatment device 22, the Full-automatic water treatment device 22
It is connected to the end to intake on economizer 24 by feed pump 23,24 upper water-out mouth end of the economizer is connected to the water inlet end of boiler 13.
Sulfur removal technology principle：After flue gas enters desulfuring and denitrifying apparatus 29 obliquely by import, flowed up from bottom of tower, desulfurization
Denitrification apparatus 29 is furnished with three layers of spraying layer, is sprayed by nozzle, forms the atomized drop that particle is tiny, reactivity is very high, covers
Lid rate is more than 200%.This technique uses advanced silicon carbide spiral nozzle, under same spray condition, is needed to the pressure of pump
Ask relatively low.The arrangement of spraying layer increases the contact area and probability of slurries and gas, ensures that absorption tower cross section can be complete
It is covered with, SO2, SO3, HF, HCl etc. is made to be sufficiently removed.Due to passing through circulating pump in 29 inner absorbent slurries of desulfuring and denitrifying apparatus
Iterative cycles and smoke contacts, absorbent utilization rate are high.
Flue gas by purified treatment flows through two-stage demister, and the slurries droplet that flue gas is carried removes.Divide from flue gas
It separates out the droplet come and is slowly condensed into bigger drop, then slid down along the lower part of demister blade.
Due to providing good gas-liquid contact condition in desulfuring and denitrifying apparatus 29, the sulfur dioxide of flue gas body is by alkalies
The effect that body absorbs is good；Grit in flue gas is also easily adhered to by water mist and is removed, to make air-flow take the grit and droplet of tower out of
Seldom.
Flue gas tangentially enters 29 bottom of desulfuring and denitrifying apparatus, rises in tower and experience sprays denitration successively.Most afterwards through washing
The flue gas washed and purified is emptied by chimney.
It is furnished with NaClO in absorption tower2Slurries are got to spraying layer by slurry circulating pump, circulating pump, are sprayed by nozzle, formation
The atomized drop that grain is tiny, reactivity is very high.This technique uses international advanced nozzle, right under same spray condition
The pressure demand of pump is relatively low.The arrangement of spraying layer increases the contact area and probability of slurries and gas, ensures that absorption tower is transversal
Face can be covered with completely, and NOX etc. is made fully to be removed.Since absorption tower inner absorbent slurries pass through circulating pump iterative cycles and cigarette
Gas contacts, and absorbent utilization rate is high.
It although an embodiment of the present invention has been shown and described, for the ordinary skill in the art, can be with
Understanding without departing from the principles and spirit of the present invention can carry out these embodiments a variety of variations, modification, replace
And modification, the scope of the present invention is defined by the appended.
Claims (3)
1. a kind of 500KW mobile containers biomass power generation system, including boiler container system (1), boiler auxiliaries
Container system (2) and steam turbine and its ancillary equipment container system (3), it is characterised in that：The boiler container system
(1) include charger (11), burner (12), boiler (13), divide drum (14) and recycling pond (15), the charger (11)
One end in boiler container, the discharge port end connection burner (12) of the charger (11), the burner (12)
Outlet end connects boiler (13), a certain amount of demineralized water is housed in the boiler (13), and the steam drain end of boiler (13) is fixed
It is communicated with a point drum (14), the venthole for dividing drum (14) fixes connection steam turbine and its ancillary equipment container system
(3) steam turbine (32), the steam turbine and its ancillary equipment container system (3) include generator (31), steam turbine (32),
Fuel tank (33), condenser (34), condensate pump (35) and water circulating pump (36), the drive shaft end of the steam turbine (32), which is fixed, to be connected
Sending and receiving motor (31), and the steam output end of steam turbine (32) fixes connection condenser (34) by pipeline, the condenser (34)
Hot well is drawn through a manifold, is divided to two-way to two condensate pump (35) entrances, and two condensate pumps (35) pass through pipeline
Connection recycling pond (15), the recycling pond (15) are connected to boiler (13), the burner (12) by water circulating pump (36)
Exhanst gas outlet by pipeline connect boiler auxiliaries container system (2) economizer (24), the economizer (24)
Outlet port is connected to bag filter (27), and compressed air reservoir (25), the pressure are communicated in the bag filter (27)
Contracting air reservoir (25) is equipped with air compressor (26), and the outlet side of bag filter (27) is connected to by air-introduced machine (28)
Desulfuring and denitrifying apparatus (29), the desulfuring and denitrifying apparatus (29) are equipped with chimney (210), boiler auxiliaries container system
One end of system (2) is fixed with water tank (21), water tank (21) the connection Full-automatic water treatment device (22), the full-automatic water
Processing unit (22) is connected to the end to intake on economizer (24) by feed pump (23), and economizer (24) the upper water-out mouth end connects
The water inlet end of logical boiler (13).
2. a kind of 500KW mobile containers biomass power generation system according to claim 1, it is characterised in that：It is described
Charger (11) fuel is biomass block, and grain size is no more than 10mm.
3. a kind of 500KW mobile containers biomass power generation system according to claim 1, it is characterised in that：It is described
Three layers of spraying layer are equipped in desulfuring and denitrifying apparatus (29), and desulfuring and denitrifying apparatus (29) bottom end is communicated with slurries pump (211), it is described
Using the nozzle of round inlet zone in spraying layer, hydrojet is conical hollow shape, and spray angle is 60-120 °.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810506482.6A CN108518255A (en) | 2018-05-24 | 2018-05-24 | A kind of 500KW mobile containers biomass power generation system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810506482.6A CN108518255A (en) | 2018-05-24 | 2018-05-24 | A kind of 500KW mobile containers biomass power generation system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108518255A true CN108518255A (en) | 2018-09-11 |
Family
ID=63427396
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810506482.6A Pending CN108518255A (en) | 2018-05-24 | 2018-05-24 | A kind of 500KW mobile containers biomass power generation system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108518255A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109883046A (en) * | 2019-03-29 | 2019-06-14 | 上海工业锅炉(无锡)有限公司 | A kind of large capacity moving heat source and its operating method |
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| CN103075723A (en) * | 2013-01-29 | 2013-05-01 | 嘉兴新嘉爱斯热电有限公司 | Method for forming biomass fuel by comprehensively utilizing straws |
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2018
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| CN201277065Y (en) * | 2008-10-29 | 2009-07-22 | 郭清温 | Biomass generator |
| CN102191956A (en) * | 2010-03-04 | 2011-09-21 | 天华化工机械及自动化研究设计院 | Method for reducing coal consumption of coal fired power plant by arranging steam pipe type drying system |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN109883046A (en) * | 2019-03-29 | 2019-06-14 | 上海工业锅炉(无锡)有限公司 | A kind of large capacity moving heat source and its operating method |
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Application publication date: 20180911 |