CN104235817B - The coal of fan mill and air swept mill powder process and the green electricity generation system of mud multifuel combustion - Google Patents
The coal of fan mill and air swept mill powder process and the green electricity generation system of mud multifuel combustion Download PDFInfo
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- CN104235817B CN104235817B CN201410522356.1A CN201410522356A CN104235817B CN 104235817 B CN104235817 B CN 104235817B CN 201410522356 A CN201410522356 A CN 201410522356A CN 104235817 B CN104235817 B CN 104235817B
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- 239000000843 powder Substances 0.000 title claims abstract description 110
- 239000003245 coal Substances 0.000 title claims abstract description 76
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 23
- 238000000034 method Methods 0.000 title claims abstract description 19
- 230000005611 electricity Effects 0.000 title claims abstract description 16
- 230000008569 process Effects 0.000 title claims abstract description 16
- 239000010802 sludge Substances 0.000 claims abstract description 39
- 238000001035 drying Methods 0.000 claims abstract description 27
- 238000007599 discharging Methods 0.000 claims abstract description 19
- 235000012054 meals Nutrition 0.000 claims abstract description 4
- 239000007789 gas Substances 0.000 claims description 44
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 19
- 239000003546 flue gas Substances 0.000 claims description 19
- 239000008399 tap water Substances 0.000 claims description 17
- 235000020679 tap water Nutrition 0.000 claims description 17
- 238000002156 mixing Methods 0.000 claims description 15
- 230000008676 import Effects 0.000 claims description 13
- 238000004519 manufacturing process Methods 0.000 claims description 11
- 239000000779 smoke Substances 0.000 claims description 11
- 239000004566 building material Substances 0.000 claims description 9
- 238000009434 installation Methods 0.000 claims description 6
- 235000019504 cigarettes Nutrition 0.000 claims description 4
- 238000000605 extraction Methods 0.000 claims description 3
- 239000002274 desiccant Substances 0.000 claims description 2
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- 239000003344 environmental pollutant Substances 0.000 abstract description 7
- 231100000719 pollutant Toxicity 0.000 abstract description 7
- 238000010248 power generation Methods 0.000 abstract description 4
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- 239000002893 slag Substances 0.000 abstract description 2
- 238000005516 engineering process Methods 0.000 description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 239000002918 waste heat Substances 0.000 description 7
- 239000002817 coal dust Substances 0.000 description 6
- 238000011161 development Methods 0.000 description 6
- 238000005265 energy consumption Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 238000005422 blasting Methods 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 230000008859 change Effects 0.000 description 2
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- 230000006378 damage Effects 0.000 description 2
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- 238000003916 acid precipitation Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 239000002802 bituminous coal Substances 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
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- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
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- 230000029087 digestion Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000005431 greenhouse gas Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
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Classifications
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- 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
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/12—Heat utilisation in combustion or incineration of waste
-
- 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
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/14—Combined heat and power generation [CHP]
-
- 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
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
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- Treatment Of Sludge (AREA)
Abstract
The invention discloses coal and the green electricity generation system of mud multifuel combustion of a kind of fan mill and air swept mill powder process, comprise boiler, air swept mill, closed sludge bin, fan mill, drying tube, gas powder separator, apparatus for recovering, Powder discharging fan, weary gas blower fan, the second machine supplying powder, the second air and powder mixer; Described closed sludge bin is connected to the charging aperture of drying tube, the discharging opening of drying tube connects the charging aperture of gas powder separator through fan mill, the weary gas outlet of gas powder separator is connected to the air inlet of the second air and powder mixer successively through apparatus for recovering, weary gas blower fan, the meal outlet of described gas powder separator is connected to the powder inlet of the second air and powder mixer through the second machine supplying powder, the second air and powder mixer connects the burner of boiler again.Native system achieves coal fired power generation, sludge drying, sludge incineration, pollutant integration remove, the combination of utilization of ash and slag, Turbine Cold Junction UTILIZATION OF VESIDUAL HEAT IN, makes coal-mud hybrid power system have the function of efficient, energy-conservation, economy, environmental protection.
Description
Technical field
The invention belongs to technical field of power generation, particularly relate to coal and mud multifuel combustion generation technology.
Background technology
Comrade Xi Jinping points out: energy security is of overall importance, the strategic problem of relation national economy social development, develops, people's lives are improved, social long-term stability is most important to national prosperity.In the face of energy supply and demand general layout new change, international energy new development trend, ensure national energy security, production of energy and consumption revolution must be promoted.Promotion production of energy and consumption revolution are long-range strategies, must do, Expedite the application key task and major action from current.Promote energy technology revolution, upgrading of driving the industry.Base oneself upon China's national situation, immediately following international energy technological revolution new trend, take green low-carbon as direction, classification promotes technological innovation, re-invent industry, business model innovation, and combine closely with other field new and high technology, energy technology and association Industry Cultivation thereof are become to drive the new growing point of CHINESE INDUSTRIES upgrading.
The resources and environment problem that burning of coal and utilization cause, is a difficult problem for whole world facing, causes the extensive attention of international community.As primary energy, the Land use systems of coal mainly burns in China, and burning of coal is the greatest contamination source of causing China's environmental destruction.The energy-consuming of China accounts for 8 ~ 9% of the world, but SO
2discharge accounts for 15.1% of the world, and total emission volumn has reached 2,346 ten thousand tons in 1997, accounts for No. 1 in the world; NOx accounts for 10.1%, CO of the world
2account for 9.6%.The wherein SO that discharges of China's coal combustion
2account for 87%, CO of the total discharge in the whole nation
2account for 71%, NOx and account for 67%, dust accounts for 60%.SO coal fire discharged in a large number
2great harm is defined in China with NOx.Acid rain region expands rapidly, has exceeded 40% of area.Cause economy difficult to the appraisal and social loss.In addition, the coal-fired greenhouse gases CO discharged
2total amount also occupies second place of the world.
Burn the important factor in order that the pollution that causes of coal has become restriction Chinese national economy and social sustainable development, already become in the world, particularly neighboring countries and regions focus that China is paid close attention to.If do not taked strong control measures, this situation will be accelerated to worsen, and directly affects the state plans in China 1,200,000,000 population health and protection 1,600,000,000 arable land.
Rich coal resources in China, petroleum resources is deficient, and the accounting of new forms of energy in energy consumption structure is also very low.Such energy resource structure determines China in considerable time from now on, and coal fired power generation is still in the principal status of public economy.But the coal resources of China and distribution of water resources are extremely unbalanced, coastal region in east China water resource is enriched, and coal resources reserves are few; West area rich coal resources, but water resource there is a serious shortage in the supply, ecological environment is extremely fragile.And east middle part densely populated, ecological environment bearing space is limited, be country determine control consumption of coal, air conservation key area.Day by day harsh coal-burning power plant's energy-saving and emission-reduction requirement, coal-burning power plant is developed, particularly in the coastal region in east China, be subject to increasing restriction, develop new pollution that caused by coal burning thing control technology, the degree of depth is energy-conservation becomes very urgent with utilization of waste as resource technology.
At present, the pollutant catabolic gene of coal-burning power plant mainly comprises desulphurization and denitration, dedusting and carbon dioxide control.Desulfurization extensively adopts limestone-gypsum method; Denitration technology mainly comprises low NOx combustion, SNCR and SCR technology; Dedusting extensively adopts common electric precipitation and wet-esp technology; Carbon dioxide controls to comprise the links such as separation, storage and recycling, is mainly in development at present, not yet extensive extensive use.Above-mentioned technology mainly adopts the thinking of dividing and rule to pollutant, system complex, and processing cost is higher.Develop integrated pollutant removing and resourcable transformation technology, various pollutant is made to remove under lower financial cost and to be converted into useful product, a kind of green generation technology of zero-emission is become, the application space of expansion coal-fired power generator set by promoting coal-fired power generator set.
In the raising coal-burning power plant thermal efficiency, the maximum heat loss of current condensing-type power plant is condenser cold junction heat loss, can reach more than 50% of coal-fired thermal discharge.Because condenser circulating water outlet temperature is not high, although waste heat amount is very large, grade is very low, generally utilizes at present; By contrast, the thermal efficiency of thermal power plant unit then improves greatly, and cogeneration becomes one of effective technology improving efficiency of energy utilization, but in the non-heat supply phase, still has a large amount of waste heat taken away by condenser recirculated water and lose.
Municipal sludge is the inevitable outcome of sewage treatment plant and sewage disposal.Without after the mud entered environment that appropriate process is disposed, bring secondary pollution directly to water body and air, not only reduce the effective processing capacity of sewage disposal system, and serious threat is constituted to the activity of ecological environment and the mankind.China produces now the existing treatment facility of a large amount of municipal sludges every year and is less than 1/4, and it is also few for counting that existing sludge digestion tank can normally run, and some does not just run at all.The mud in some place does not obtain rational treatment and disposal and just directly discharges, and causes serious secondary pollution.Owing to containing the harmful substances such as plurality of heavy metal in mud, it is unsafe for directly carrying out landfill stabilization, and can take a large amount of land resource.Heat treatment has become the effective technology solving municipal sludge problem, the mainly burning method of extensive use at present, namely mud to be dewatered and after drying and other treatment, deliver to Wei Fei center to be burned by grate furnace, rotary kiln and fluidized bed incinerator etc., or deliver in power plant and carry out multifuel combustion with coal.The subject matter existed in sludge incineration is that sludge drying energy consumption is high, system complex, and sludge incineration treating capacity is little, can not meet the needs that municipal sludge is disposed completely.The Disposal System of Mud Burning of exploitation Large Copacity low energy consumption, is still the important topic of current field of Environment Protection.
The feature needing contrary distribution is produced according to coal resources, Bei Meinan send, transferring electricity from the west to the east is that the important energy source that China's energy development strategy is determined flows to, Midwest coal resources enrichment area rational deployment eastwards middle part power transmission large-scale coal-electricity base, being the important handgrip implementing national energy development strategy, is be conducive to the energy resources realized in larger scope to distribute rationally.But in recent years, along with transregional power transmission scale constantly expands, the large-scale coal-electricity base water resources shortage contradiction more fragile with ecological environment will be more and more outstanding.
Summary of the invention
Technical problem to be solved by this invention be to provide a kind of can either carry out in Large Copacity high parameter coal-burning power plant extensive low-power consumption sludge dry and burn, ash comprehensive utilization can also be realized, turbine discharge UTILIZATION OF VESIDUAL HEAT IN, flue gas pollutant integration remove the system with resourcable transformation.This system is based on the cascade utilization of resource circulation utilization and energy, with coal-fired and combustion mud to the technological system of generating being combined into target, this system can realize the combined cycle target of the accumulating of solids closed, municipal sludge burning, efficient fuel coal, flue gas resource, zero-emission, no pollution, weary gas warm water, overcomes the deficiency existed in existing conventional coal-burning power plant and sludge incineration factory.
For solving the problems of the technologies described above, the present invention adopts following technical scheme:
The coal of a kind of fan mill and air swept mill powder process and the green electricity generation system of mud multifuel combustion, comprise boiler, closed coal bunker, coal bunker, feeder, air swept mill, mill separator, pulverized-coal collector, spiral powder conveying machine, Pulverized Coal Bin, the first machine supplying powder, the first air and powder mixer, steam turbine and chimney, described closed coal bunker, coal bunker, feeder, air swept mill, mill separator, pulverized-coal collector, spiral powder conveying machine, Pulverized Coal Bin, first machine supplying powder, first air and powder mixer, the burner of boiler connects successively, the steam (vapor) outlet of described boiler connects the steam inlet of steam turbine, it is characterized in that: also include closed sludge bin, fan mill, drying tube, gas powder separator, apparatus for recovering, Powder discharging fan, weary gas blower fan, second machine supplying powder, second air and powder mixer, tap water heater, closed ash silo, building materials manufacturing installation, denitration integrated device,
Described closed sludge bin is connected to the charging aperture of drying tube, the discharging opening of drying tube connects the charging aperture of gas powder separator through fan mill, the weary gas outlet of gas powder separator is connected to the air inlet of the second air and powder mixer successively through apparatus for recovering, weary gas blower fan, the meal outlet of described gas powder separator is connected to the powder inlet of the second air and powder mixer through the second machine supplying powder, the mixed export of the second air and powder mixer connects the burner of boiler;
The steam (vapor) outlet of described steam turbine connects the thermal source import of tap water heater, and the thermal source outlet of tap water heater connects back boiler again;
The furnace hopper of described boiler bottom connects closed ash silo, and described closed ash silo connects building materials manufacturing installation again;
The flue afterbody of described boiler is provided with deduster, and described deduster is connected to the dirty gas import of denitration integrated device, described denitration integrated device gas outlet one road is connected to chimney, another road is connected to closed coal bunker.
In the specific embodiment of the present invention, be provided with mixing chamber outside described boiler, the mixed flue gas outlet of mixing chamber is connected to the dry gas entrance of drying tube, and the hot cigarette import of mixing chamber is connected to the high-temperature flue gas extraction opening on the flue of boiler; Described house outlet also connects cold smoke blower fan, and described cold smoke blower fan is connected to the cold smoke import of mixing chamber.
In the detailed description of the invention of invention, the flue of described boiler is also provided with air preheater before being positioned at deduster, and the air intlet of described air preheater connects pressure fan, and air outlet slit divides two-way, and a road is connected to burner, and a road is connected to that air swept mill.
Adopt technique scheme, native system by arranging closed warehouse of sludge and coal bunker, therefore can avoid mud stink and coal dust to the diffusion of atmospheric environment; Mud drying pipe in warehouse of sludge is with high-temperature flue gas/black furnace cigarette blending agent contacts by preliminarily dried, enter in the lump in mud lapping device and be milled to very thin particle diameter, and carry out degree of depth heat exchange with drying medium, moisture in mud declines to a great extent, the primary mixture ground carries out after the separation of gas powder through gas powder separator, and the high weary gas containing wetting is re-used as powder feeding medium and dewatered sludge is sent into boiler combustion after apparatus for recovering cooling condensation reduction humidity.In this process, mud and high-temperature flue gas carry out direct contact heat transfer, speed and the treating capacity of drying sludge can be significantly improved, reclaim the waste heat of dry weary gas, reduce energy consumption for drying, and reduce the moisture that mud brings boiler into, thus reduce boiler export flue gas dew point temperature and heat loss due to exhaust gas, improve boiler thermal output; Because oxygen content in flue gas is very low, therefore the security of drying system can be guaranteed, avoid blasting.Native system is by arranging denitration integrated device, SOx, NOx and the CO in flue gas
2remove.Native system, by arranging turbine discharge residual heat using device, utilizes turbine discharge waste-heat city tap-water, improves tap water temperature, thus reduces the fuel of city dweller's heating tap water consumption; Two of its preferred scheme is in the coastal area lacking fresh water, with the cooling medium of seawater as turbine discharge, that is to say and uses turbine discharge as the heat source of desalinization, prepare fresh water by low-temperature evaporation desalination technology.No matter be which kind of scheme, all can produce huge energy-saving effect.
Also be provided with ash comprehensive utilization device in this system, its preferred scheme utilizes the lime-ash of boiler emission to manufacture building materials.
Therefore, the coal of the fan mill that proposes of the present invention and air swept mill powder process and the green electricity generation system of mud multifuel combustion have that mud handling capacity is large, system thermal efficiency is high, comprehensive utilization of resources, green non-pollution advantage.
Accompanying drawing explanation
Fig. 1 is system architecture schematic diagram of the present invention.
Detailed description of the invention
As shown in Figure 1, in the coal and the green electricity generation system of mud multifuel combustion of fan mill of the present invention and air swept mill powder process, closed warehouse of sludge 1 is connected to the charging aperture of drying tube 3 through sludge conveyer 2, the discharging opening of drying tube 3 is connected to fan mill 4, fan mill 4 is connected to the charging aperture of gas powder separator 5, the weary gas outlet of gas powder separator 5 is connected to apparatus for recovering 6, apparatus for recovering 6 is connected to weary gas blower fan 7, weary gas blower fan 7 is connected to the air inlet of the second air and powder mixer 8, the powder outlet of gas powder separator bottom is connected to the second machine supplying powder 10, second machine supplying powder 10 is connected to the powder inlet of the second air and powder mixer 8.The discharging opening of the second air and powder mixer 8 is connected to the burner 9 of boiler 18.
The desiccant inlet of drying tube 3 and the mixed flue gas outlet of mixing chamber 11, the outlet flue that hot cigarette import is connected to the high-temperature flue gas extraction opening 17 of boiler 18, the cold smoke import of mixing chamber 11 is connected to cold smoke blower fan 12 of mixing chamber 11, the mouth that enters of cold smoke blower fan 12 is connected with the outlet of deduster 13.
Closed coal bunker 14 is connected to coal bunker 15, coal bunker 15 is connected to feeder 16, feeder 16 is connected to that air swept mill 33, air swept mill 33 is connected to mill separator 34, mill separator 34 is connected to pulverized-coal collector 35, the meal outlet of pulverized-coal collector 35 is connected to commutator 36, commutator 36 is connected to spiral powder conveying machine 37, spiral powder conveying machine 37 is connected to Pulverized Coal Bin 38, Pulverized Coal Bin 38 is connected to the first machine supplying powder 39, first machine supplying powder 39 is connected to the powder inlet of the first air and powder mixer 40, and the discharging opening of the first air and powder mixer 40 is connected to the burner 9 of boiler 18.
The air inlet of the first air and powder mixer 40 is connected to the air outlet of Powder discharging fan 41, and the air inlet of Powder discharging fan 41 is also connected to the weary gas outlet of pulverized-coal collector 35, First air pipeline 29 and cold air duct 31, and cold air duct 31 is connected to the air outlet of pressure fan 28.
The steam (vapor) outlet of boiler 18 connects the steam inlet of steam turbine 19, and the steam inlet of steam turbine 19 is connected to the thermal source import of tap water heater 20, and the thermal source import of tap water heater 20 connects back boiler 18.
The lower furnace portion furnace hopper 21 of boiler 18 is connected to closed ash silo 22 and connects, and closed ash silo 22 is connected to building materials manufacturing installation 23.
The flue afterbody of boiler 18 is positioned at deduster 13 anterior position and arranges air preheater 24.The air outlet of deduster 13 divides two-way, and a road is connected to the dirty gas import of denitration integrated device 25, and what another road connected cold smoke blower fan 12 enters mouth.
Air preheater 24 air inlet is connected to pressure fan 28, the air outlet of air preheater 24 is connected respectively to that air swept mill 33 and the air inlet of Powder discharging fan 41 by two branch pipe(tube)s of First air pipeline 29 and First air pipeline 29, and air preheater 24 is also connected with the burner 9 of boiler 18 by Secondary Air pipeline 30.
The air outlet of pressure fan 28 also by pipeline 31 respectively be connected to exhaust fan 41 and air swept mill 33 two branch pipe(tube)s of First air pipeline 29 converge.
Closed warehouse of sludge 1 is also directly connected to boiler-burner 9 by pipeline 32.
The exhaust outlet of denitration integrated device 25 divides two-way, and a road connects chimney 17 through air-introduced machine 25, and another road is connected to closed coal bunker 14 through pipeline 42.
Should be based on fan mill of comprehensive utilization of resources and the coal of air swept mill powder process and the operation principle of the green electricity generation system of mud multifuel combustion:
Be stored in the mud in closed warehouse of sludge 1, drying tube 3 is transported to through sludge conveyer 2, to contact with the drier from mixing chamber 11 and by preliminarily dried, then fan mill 4 is entered in the lump with drier, mud is further dried and is ground to regulation particle diameter, the wind powder mixture ground enters gas powder separator 5 and is separated, after being separated, the high weary gas that wets that contains enters cooled condensation in apparatus for recovering 6, it is released heat and is recovered, weary gas after dehumidifying is as powder feeding medium, in the second air and powder mixer 8 with gas powder separator 5 bottom connect the dewatered sludge powder that the second machine supplying powder 10 sends here and mix, and be delivered to the burner 9 of boiler 18.The gas that in closed warehouse of sludge 1, sludge fermentation produces also delivers to burner combustion by pipeline 32.
Be stored in the raw coal in closed coal bunker 14, be admitted to coal bunker 15, send into through feeder 16 that air swept mill 33, the wind powder mixture conveying mill separator 34 of 33 outlets that air swept mill, bulky grain turns back to that air swept mill 33 after being separated, all the other wind powder mixtures enter pulverized-coal collector 35, the isolated coal dust of pulverized-coal collector 35 sends into Pulverized Coal Bin 38 through spiral powder conveying machine 37, coal dust in Pulverized Coal Bin 38 enters the first air and powder mixer 40 through the first machine supplying powder 39, by the powder feeding medium transport exported from Powder discharging fan 41 to boiler-burner 9.Weary gas after coal dust isolated by pulverized-coal collector 35 enters Powder discharging fan 41 with from forming powder feeding medium after the hot blast of First air pipeline 29 and the cold wind mixing temperature adjustment of cold air duct 31.Closed coal bunker 14 is connected with denitration integrated device 25, uses isolated CO in denitration integrated device 25
2deactivation protection is carried out to closed coal bunker 14.
Pressure fan 28 sucks air from environment, after air preheater 24 heats, a part by First air pipeline 29 with from the cold wind mixing temperature adjustment of cold air duct 31 laggard enter air swept mill 33, another part directly delivers to boiler-burner 9 by Secondary Air pipeline 30.
The gas produced in dewatered sludge, coal dust, closed warehouse of sludge mixes with air, burns in boiler 18, liberated heat is for the production of steam, steam discharge after steam enters steam turbine 19 acting enters tap water heater 20, and the cold water from waterworks is returned running water system by after turbine discharge waste-heat.
Boiler export flue gas, after dust removed by deduster 13, enters in denitration integrated device 25, SOx, NOx in flue gas is removed, and remaining clean innocuous gas enters chimney 27 through air-introduced machine 26 and discharges.SOx, NOx of removing are used as to make waste material.
Enter closed ash silo 22 from the lower furnace portion furnace hopper 21 solid-state lime-ash out of boiler 18, be then sent in building materials manufacturing installation 23 and make building materials.
Native system achieves coal fired power generation, sludge drying, sludge incineration, pollutant integration remove, the combination of utilization of ash and slag, Turbine Cold Junction UTILIZATION OF VESIDUAL HEAT IN, makes coal-mud hybrid power system have the function of efficient, energy-conservation, economy, environmental protection.This coal and the green electricity generation system patent of mud multifuel combustion have following characteristics:
(1) system support uses fan mill system with air swept mill, is applicable to the multifuel combustion of mud and anthracite, meager coal or bituminous coal.
(2) in this system, mud and high-temperature flue gas carry out direct contact heat transfer, the speed of drying sludge can be significantly improved, reclaim the waste heat of dry weary gas, reduce energy consumption for drying, and reduce the moisture that mud brings boiler into, thus reduce boiler export flue gas dew point temperature and heat loss due to exhaust gas, improve boiler thermal output; Because oxygen content in flue gas is very low, therefore the security of drying system can be guaranteed, avoid blasting.
(3) the Treatment of Sludge ability of this system can reach more than 100t/h, is significantly higher than the level of current sludge incinerator day output 300-600t/d.
(4) be provided with closed warehouse of sludge and coal bunker in this system, therefore mud stink and coal dust can be avoided to the diffusion of atmospheric environment, improve environment.
(5) be provided with denitration integrated device, this device removes SOx, the NOx in flue gas, and what enter smoke stack emission is clean harmless nitrogen and oxygen.SOx, NOx of removing can be used as to make waste material.
(6) be provided with tap water heater in this system, utilize turbine discharge waste-heat city tap-water, improve tap water temperature, thus reduce the fuel of city dweller's heating tap water consumption, there is significant energy-saving effect.
(7) be also provided with ash comprehensive utilization device in this system, the lime-ash of boiler emission can be utilized to manufacture building materials, strengthen the comprehensive utilization of resource.
But; those skilled in the art will recognize that; above-mentioned detailed description of the invention is exemplary; to better enable those skilled in the art understand this patent; can not be interpreted as it is restriction to this patent protection domain; as long as according to this patent disclose any equivalent change done or the modification of spirit, all fall into the scope of this patent protection.
Claims (7)
1. the coal of a fan mill and air swept mill powder process and the green electricity generation system of mud multifuel combustion, comprise boiler, closed coal bunker, coal bunker, feeder, air swept mill, mill separator, pulverized-coal collector, spiral powder conveying machine, Pulverized Coal Bin, the first machine supplying powder, the first air and powder mixer, Powder discharging fan, steam turbine; Described closed coal bunker, coal bunker, feeder, air swept mill, mill separator, pulverized-coal collector, spiral powder conveying machine, Pulverized Coal Bin, the first machine supplying powder connect successively, described first machine supplying powder is connected to the powder inlet of the first air and powder mixer, the weary gas outlet of pulverized-coal collector connects Powder discharging fan, Powder discharging fan connects the air inlet of the first air and powder mixer again, the discharging opening of the first wind powder gaseous mixture connects the burner of boiler, and the steam (vapor) outlet of described boiler connects the steam inlet of steam turbine; Also include closed sludge bin, fan mill, drying tube, gas powder separator, apparatus for recovering, weary gas blower fan, the second machine supplying powder, the second air and powder mixer;
Described closed sludge bin is connected to the charging aperture of drying tube, the discharging opening of drying tube connects the charging aperture of gas powder separator through fan mill, the weary gas outlet of gas powder separator is connected to the air inlet of the second air and powder mixer successively through apparatus for recovering, weary gas blower fan, the meal outlet of described gas powder separator is connected to the powder inlet of the second air and powder mixer through the second machine supplying powder, the mixed export of the second air and powder mixer connects the burner of boiler; It is characterized in that: also comprise tap water heater, closed ash silo, building materials manufacturing installation, denitration integrated device;
The steam (vapor) outlet of described steam turbine connects the thermal source import of tap water heater, and the thermal source outlet of tap water heater connects back boiler again;
The furnace hopper of described boiler bottom connects closed ash silo, and described closed ash silo connects building materials manufacturing installation again;
The flue afterbody of described boiler is provided with deduster, and described deduster is connected to the dirty gas import of denitration integrated device, described denitration integrated device gas outlet one road is connected to chimney, another road is connected to closed coal bunker.
2. the coal of fan mill according to claim 1 and air swept mill powder process and the green electricity generation system of mud multifuel combustion, it is characterized in that: outside described boiler, be provided with mixing chamber, the mixed flue gas outlet of mixing chamber is connected to the desiccant inlet of drying tube, and the hot cigarette import of mixing chamber is connected to the high-temperature flue gas extraction opening of boiler; Described house outlet also connects cold smoke blower fan, and described cold smoke blower fan is connected to the cold smoke import of mixing chamber.
3. the coal of fan mill according to claim 2 and air swept mill powder process and the green electricity generation system of mud multifuel combustion, it is characterized in that: the flue of described boiler is also provided with air preheater before being positioned at deduster, the air inlet of described air preheater connects pressure fan, air outlet divides two-way, one road is connected to burner, and another road is connected to that air swept mill.
4. the coal of fan mill according to claim 3 and air swept mill powder process and the green electricity generation system of mud multifuel combustion, is characterized in that: another road of the air outlet of described air preheater is also connected to Powder discharging fan.
5. the coal of fan mill according to claim 3 and air swept mill powder process and the green electricity generation system of mud multifuel combustion, is characterized in that: described pressure fan is also connected to by pipeline that air swept mill and Powder discharging fan.
6. the coal of the fan mill according to the arbitrary claim of claims 1 to 3 and air swept mill powder process and the green electricity generation system of mud multifuel combustion, is characterized in that: described closed sludge bin is also directly connected to the burner of boiler by pipeline.
7. the coal of fan mill according to claim 1 and air swept mill powder process and the green electricity generation system of mud multifuel combustion, is characterized in that: described apparatus for recovering and described tap water heater are heat exchanger.
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| CN105042610A (en) * | 2015-07-27 | 2015-11-11 | 四川川锅锅炉有限责任公司 | CFB oxygen-enriched combustion smoke near zero emission power generation system |
| CN112094029A (en) * | 2020-09-16 | 2020-12-18 | 山东达源环保工程有限公司 | Hollow blade sludge drying system and method |
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Inventor after: Shi Dazhong Inventor after: Shi Dengyu Inventor after: Wang Bo Inventor before: Shi Dazhong Inventor before: Pei Yufeng Inventor before: Shi Dengyu Inventor before: Wang Bo Inventor before: Wang Yining Inventor before: Yao Yuge |
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