CN204114954U - The efficient CIU of municipal refuse of low corrosion - Google Patents
The efficient CIU of municipal refuse of low corrosion Download PDFInfo
- Publication number
- CN204114954U CN204114954U CN201420590559.XU CN201420590559U CN204114954U CN 204114954 U CN204114954 U CN 204114954U CN 201420590559 U CN201420590559 U CN 201420590559U CN 204114954 U CN204114954 U CN 204114954U
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- burner
- ciu
- efficient
- fire grate
- charging aperture
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- 238000005260 corrosion Methods 0.000 title claims abstract description 39
- 230000007797 corrosion Effects 0.000 title claims abstract description 39
- 238000002485 combustion reaction Methods 0.000 claims abstract description 78
- 239000010813 municipal solid waste Substances 0.000 claims abstract description 26
- 238000010411 cooking Methods 0.000 claims abstract description 18
- 238000000855 fermentation Methods 0.000 claims abstract description 18
- 230000004151 fermentation Effects 0.000 claims abstract description 17
- 238000009434 installation Methods 0.000 claims abstract description 15
- 238000004891 communication Methods 0.000 claims abstract description 5
- 239000007787 solid Substances 0.000 claims description 72
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 32
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 31
- 239000003546 flue gas Substances 0.000 claims description 31
- 239000003245 coal Substances 0.000 claims description 18
- 239000002918 waste heat Substances 0.000 claims description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 6
- 229910052760 oxygen Inorganic materials 0.000 claims description 6
- 239000001301 oxygen Substances 0.000 claims description 6
- 239000007789 gas Substances 0.000 claims description 3
- 238000000034 method Methods 0.000 description 25
- 230000008569 process Effects 0.000 description 22
- 230000000694 effects Effects 0.000 description 16
- 235000017168 chlorine Nutrition 0.000 description 12
- 239000000460 chlorine Substances 0.000 description 11
- 238000010438 heat treatment Methods 0.000 description 11
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 10
- 229910052801 chlorine Inorganic materials 0.000 description 10
- 239000002893 slag Substances 0.000 description 8
- 238000013461 design Methods 0.000 description 6
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 6
- 150000001875 compounds Chemical class 0.000 description 5
- 238000001035 drying Methods 0.000 description 5
- 230000005855 radiation Effects 0.000 description 5
- 238000012546 transfer Methods 0.000 description 5
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- 230000008901 benefit Effects 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000010304 firing Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 238000002309 gasification Methods 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical group [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 125000001309 chloro group Chemical class Cl* 0.000 description 2
- 239000002361 compost Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 238000006477 desulfuration reaction Methods 0.000 description 2
- 230000023556 desulfurization Effects 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 238000004056 waste incineration Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 206010020843 Hyperthermia Diseases 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000012717 electrostatic precipitator Substances 0.000 description 1
- 230000036031 hyperthermia Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
Classifications
-
- 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
Landscapes
- Incineration Of Waste (AREA)
Abstract
The utility model discloses a kind of efficient CIU of municipal refuse of low corrosion, comprise steam generator system and the auxiliary combustion system of biogas, described steam generator system comprises the combustion chamber with cavity, and described combustion chamber has charging aperture, slag-drip opening, air inlet and exhaust outlet; The auxiliary combustion system of biogas, the auxiliary combustion system of described biogas comprises burner, dehydrating unit and for the installation for fermenting by rubbish from cooking fermentation process, described burner is connected to described combustion chamber, described burner, dehydrating unit and installation for fermenting serial communication successively.The moisture content difference of the municipal refuse efficient CIU rubbish of the low corrosion that the utility model relates to is little, and combustion heat value and moisture content are even, and corrosivity is low.
Description
Technical field
The utility model relates to treatment of urban garbage field, particularly relates to a kind of efficient CIU of municipal refuse of low corrosion.
Background technology
The year generation of China's municipal refuse has reached hundred million tonnes not, now conventional processing mode has landfill, compost, pyrolysis and burning etc., floor space wherein needed for landfill is large and pollute the environment, compost and pyrolysis require higher to the composition of rubbish and business efficiency is low, because rubbish can not only be carried out recycling treatment by waste incineration and generating electricity technology, and floor space is little, disposal ability strong, becomes the major way of solid refuse process gradually.
Applying maximum in existing waste incineration and generating electricity system is mechanical grate boiler, it is large that this boiler has treating capacity, the advantages such as the thermal efficiency is high, but because the kind of rubbish is complicated, combustion heat value and moisture content uneven, there is the insufficient problem of burning in part that in combustion process, moisture content is high, and the Cl contained in combustion process rubbish can change into HCl corrodes boiler heating surface, thus cause heating surface to lose efficacy the generation of even security incident.
Utility model content
Based on this, be necessary that the moisture content difference providing a kind of rubbish is little, combustion heat value and moisture content are even, and the efficient CIU of municipal refuse of the low low corrosion of corrosivity.
The efficient CIU of municipal refuse of low corrosion, comprises
Steam generator system, described steam generator system comprises the combustion chamber with cavity, and described combustion chamber has charging aperture, slag-drip opening, air inlet and exhaust outlet;
The auxiliary combustion system of biogas, the auxiliary combustion system of described biogas comprises burner, dehydrating unit and for the installation for fermenting by rubbish from cooking fermentation process, described burner is connected to described combustion chamber, described burner, dehydrating unit and installation for fermenting serial communication successively.
The efficient CIU of municipal refuse of the low corrosion that the utility model relates to, by the cooperation of steam generator system and the auxiliary combustion system of biogas; The burner comprised by the auxiliary combustion system of described biogas, dehydrating unit and the cooperation for the installation for fermenting by rubbish from cooking fermentation process, the moisture content avoided due to the rubbish from cooking in solid refuse is the highest, need the time of stacking process long before burning, and need absorption heat that the phenomenon of the reduction of combustion chambers burn temperature can be caused to occur owing to participating in moisture vaporization in burning process; Simultaneously also by the main source that the salinities such as the NaCl avoided in rubbish from cooking are inorganic chlorines, HCl can be changed in combustion, thus cause the phenomenon of the corrosion failure of heating surface.
The efficient CIU of municipal refuse of the low corrosion that the utility model relates to, rubbish from cooking is carried out fermentation process by the technical scheme used, the inorganic chlorine of the overwhelming majority is all stayed in zymotic fluid with the form of salinity, reduces the introducing reducing chlorine source, thus reduce the chlorine corrosion of heating surface in source; Because described burner is connected to described combustion chamber, described burner, dehydrating unit are communicated with and the design of installation for fermenting serial communication successively, described fermentation vat is used for rubbish from cooking to carry out fermentation process, the biogas produced enters burner (preposition burner and rearmounted burner) and burns after dehydrating unit, more takes full advantage of the recovery effect of the energy.
Wherein in an embodiment, described combustion chamber has the fire grate for solid refuse of banking up, and described charging aperture is communicated in described fire grate;
Also comprise feeding device, described feeding device is communicated with described charging aperture, and described feeding device is arranged between described fire grate and charging aperture, and described fire grate is communicated in described feeding device.
The efficient CIU of municipal refuse of the low corrosion that the utility model relates to, by the design of fire grate, after solid refuse through stacking process is sent to combustion chamber, what be further advanced by described feeding device is designed for control inlet amount, solid refuse is laid on above fire grate uniformly, the solid refuse entering fire grate, after the preheating and drying of First air, is convenient to carry out heat convection and radiation heat transfer under the effect of burner (preposition burner).
Wherein in an embodiment, described charging aperture, fire grate and slag-drip opening are arranged in order in the horizontal direction, and described charging aperture, fire grate and slag-drip opening are vertically in upper-lower position successively, and the plane at described fire grate place tilts toward described slag-drip opening direction.
The efficient CIU of municipal refuse of the low corrosion that the utility model relates to, by the design that fire grate tilts toward described slag-drip opening direction, be convenient to solid refuse enter fire grate afterbody and carry out last burning, solid refuse completes burnout under the effect of burner (rearmounted burner) herein, be convenient on the one hand solid refuse under gravity automatically under slide to fire grate afterbody (near slag-drip opening), cost-saving; Also the abundant after-flame of fixed fuel is made on the other hand.
Wherein in an embodiment, described burner comprises preposition burner and rearmounted burner;
Described preposition burner is all communicated with described dehumidifier by gas pipeline with rearmounted burner, described preposition burner is arranged at the inwall of described combustion chamber near the side of charging aperture and toward described fire grate, and described rearmounted burner is arranged at the inwall of described combustion chamber near the side of slag-drip opening and toward described fire grate.
The efficient CIU of municipal refuse of the low corrosion that the utility model relates to, enter the solid refuse of fire grate after the preheating and drying of First air, heat convection and radiation heat transfer is carried out under the effect of preposition burner, the gasification that solid refuse can complete volatile matter faster and the process of catching fire, following solid refuse burns along with fire grate enters central combustion district, the higher solid refuse that can make of temperature herein carries out Thorough combustion, solid refuse enters fire grate afterbody and carries out last burning subsequently, solid refuse completes burnout under the effect of rearmounted burner herein, due under the effect of preposition burner and rearmounted burner, solid refuse is more concentrated at central combustion district flame, and ignition temperature becomes higher, effectively can reduce the generation of the contaminative compounds such as bioxin in combustion process, in the process of mixed combustion, can regulate preposition burner and rearmounted burner according to characteristics such as the moisture content of the solid refuse through stacking process, volatile matter content and porositys, when moisture content height, increase the aperture of preposition burner, the methane quantity of burning in preposition burner is increased, burning produces more heat, thus the moisture in solid refuse is gasified as early as possible, solid refuse catches fire as early as possible, also increases the aperture of rearmounted burner simultaneously, makes completing smoothly of burnout, when the volatile matter content of solid refuse or porosity larger time, the aperture of preposition burner and rearmounted burner can be reduced, to save the use amount of biogas.
Wherein in an embodiment, also including feed bin and the shutoff damper for controlling feed rate, entering feed bin and being communicated in described charging aperture, described shutoff damper is movably connected on the opening and closing of described charging aperture for charging aperture.Be convenient to control feed rate, the solid refuse making at every turn to enter combustion chamber can after-flame fully.
Wherein in an embodiment, the waste heat also comprised for absorbing flue gas comes economizer and the low-pressure coal saver of heated feed water;
Described exhaust outlet is communicated with discharge duct, and described economizer, low-pressure coal saver are set in turn in described discharge duct along the flue gas discharge direction of exhaust outlet, have interval along in discharge duct flue gas discharge direction between described economizer, low-pressure coal saver.
The efficient CIU of municipal refuse of the low corrosion that the utility model relates to, described economizer is positioned at boiler flue afterbody, carrys out heated feed water for the waste heat absorbing flue gas; Described low-pressure coal saver is positioned at boiler flue afterbody, position after economizer, for carrying out degree of depth recovery, for preheating condensate water to the waste heat of flue gas.
Wherein in an embodiment, also comprise blower unit, described blower unit has air-vent and air-introduced machine, and described air-vent is communicated in the port of export of described discharge duct.
The efficient CIU of municipal refuse of the low corrosion that the utility model relates to, described blower unit is positioned at the port of export (after deduster) of described discharge duct, for increasing the fluid ability of flue gas, flue gas is by also needing further through process such as desulfurization after deduster, then enter chimney, enter in air.
Wherein in an embodiment, also comprise the Secondary Air air outlet for providing oxygen, described Secondary Air air outlet is communicated in described combustion chamber.
The secondary blast mouth of the efficient CIU of municipal refuse of the low corrosion that the utility model relates to provides the required oxygen that burns completely of solid refuse for feeding secondary wind.
Wherein in an embodiment, be provided with the water screen tube being full of recirculated water in described combustion chamber, described water screen tube is communicated with steam turbine, and described steam turbine is connected with generator.
The efficient CIU of municipal refuse of the low corrosion that the utility model relates to, the heat that incineration firing produces is for heating the water in water-cooling wall; Inner Wall of Combustion Chamber is water screen tube, is full of recirculated water in water screen tube, and become steam after recirculated water heat absorption, steam does work after entering steam turbine, and drive steam turbine to rotate, steam turbine, at drive electrical generators rotary electrification, make use of resource fully.
The efficient incinerating method of municipal refuse of the low corrosion that the utility model relates to, equipment needed thereby is simple, equipment investment is few, and easy and simple to handle, realizes the operation of automation, in solid refuse combustion process, reduce the introducing reducing chlorine source, thus reduce the chlorine corrosion of many heating surfaces, ensure that the quick ignition of the solid refuse of combustion process, smooth combustion and complete after-flame, both ensure that the safety and stability Effec-tive Function of grate boiler, again reduce the generation of the pollution compounds such as bioxin.
Accompanying drawing explanation
Fig. 1 is the efficient CIU schematic diagram of municipal refuse of the utility model embodiment low corrosion.
Description of reference numerals
1, feed bin is entered; 2, shutoff damper; 3, batch plant; 4, fire grate; 5, preposition burner; 6, fermentation vat; 7, dehumidifier; 8, Secondary Air air outlet; 9, rearmounted burner; 10, slag-drip opening; 11, slag bath is stored up; 12, burner hearth; 13, boiler flue; 14, economizer; 15, low-pressure coal saver; 16, deduster; 17, air-introduced machine; 18, chimney.
Detailed description of the invention
For the ease of understanding the utility model, below with reference to relevant drawings, the utility model is described more fully.Preferred embodiment of the present utility model is given in accompanying drawing.But the utility model can realize in many different forms, is not limited to embodiment described herein.On the contrary, provide the object of these embodiments be make the understanding of disclosure of the present utility model more comprehensively thorough.
It should be noted that, when element is called as " being fixed on " another element, directly can there is element placed in the middle in it on another element or also.When an element is considered to " connection " another element, it can be directly connected to another element or may there is centering elements simultaneously.
Unless otherwise defined, all technology used herein and scientific terminology are identical with belonging to the implication that those skilled in the art of the present utility model understand usually.The object of the term used in description of the present utility model herein just in order to describe specific embodiment, is not intended to be restriction the utility model.Term as used herein "and/or" comprises arbitrary and all combinations of one or more relevant Listed Items.
The efficient CIU of municipal refuse of low corrosion, see Fig. 1, comprises steam generator system, the auxiliary combustion system of biogas.
Described steam generator system comprises batch plant 3 and has the combustion chamber of cavity, and combustion chamber described in the present embodiment is burner hearth 12.
Described burner hearth 12 has First air air outlet (not shown), for providing the oxygen needed for burner hearth 12 combustion; Described burner hearth 12 also comprises the Secondary Air air outlet 8 for providing oxygen, and described Secondary Air air outlet 8 is communicated in described burner hearth 12.Described burner hearth 12 has charging aperture, slag-drip opening 10, air inlet (not shown) and exhaust outlet, and the exhaust outlet of described burner hearth 12 is opened on the top of burner hearth 12.Be provided with the water screen tube (not shown) being full of recirculated water in described burner hearth 12, described water screen tube is communicated with steam turbine (not shown), and described steam turbine is connected with generator (not shown).
The inside of described burner hearth 12 has feeding device, and described feeding device is batch plant 3, and described batch plant 3 is arranged at the inside of described burner hearth 12 and is communicated with described charging aperture; Described burner hearth 12 has the fire grate 4 for solid refuse of banking up, and described charging aperture is communicated in described fire grate 4; Described fire grate 4 is communicated in described batch plant 3, and described batch plant 3 is arranged between described fire grate 4 and charging aperture, and batch plant 3 described in the present embodiment is described calibrated feeder.
Described charging aperture, fire grate 4 and slag-drip opening 10 are arranged in order in the horizontal direction, and described charging aperture, fire grate 4 and slag-drip opening 10 are vertically in upper-lower position successively, and the plane at described fire grate 4 place tilts toward described slag-drip opening 10 direction.
Further, also including feed bin 1 and the shutoff damper 2 for controlling feed rate, entering feed bin 1 and being communicated in described charging aperture, described shutoff damper 2 is movably connected on the opening and closing of described charging aperture for charging aperture.Be convenient to control feed rate, the solid refuse making at every turn to enter burner hearth 12 can after-flame fully.
The auxiliary combustion system of described biogas comprises burner, dehydrating unit and for the installation for fermenting by rubbish from cooking fermentation process, and described installation for fermenting is fermentation vat 6, and described dehydrating unit is dehumidifier 7; Described burner is connected to described burner hearth 12, connection that described burner, dehydrating unit are communicated with and installation for fermenting circulates successively.
Described burner comprises preposition burner and rearmounted burner; Described preposition burner 5 is all communicated with described dehumidifier 7 by gas pipeline with rearmounted burner 9, described preposition burner is arranged at the inwall of described burner hearth 12 near the side of charging aperture and toward described fire grate 4, and described rearmounted burner is arranged at the inwall of described burner hearth 12 near the side of slag-drip opening 10 and toward described fire grate 4.Namely also described preposition burner 5 is positioned at burner hearth 12 front portion (side near charging aperture), and Main Function is the solid refuse of dry section on preheating and the described fire grate 4 that ignites, to ensure that the temperature of solid refuse reaches the demand of catching fire as early as possible.
Described rearmounted burner 9 is positioned at burner hearth 12 rear portion (side near slag-drip opening 10), for carrying out by the solid refuse entering burning-out zone burning of heating, ensures completing smoothly of combustion process; Preposition burner 5, rearmounted burner 9 all with described water screen tube at right angle setting, combustion flame direction is obliquely, towards the direction of described fire grate 4, wherein preposition burner 5 combustion flame direction is towards the front end (one end near charging aperture) of fire grate 4, and rearmounted burner 9 combustion flame direction is towards the rear end (one end near slag-drip opening 10) of fire grate 4.
The exhaust outlet of described burner hearth 12 is communicated with discharge duct (boiler flue 13), the utility model waste heat also comprised for absorbing flue gas comes economizer 14 and the low-pressure coal saver 15 of heated feed water, described economizer 14, low-pressure coal saver 15 are set in turn in described discharge duct along the flue gas discharge direction of described exhaust outlet, have interval between described economizer 14, low-pressure coal saver 15.Wherein, economizer 14 carrys out heated feed water for the waste heat absorbing flue gas, and low-pressure coal saver 15 absorbs the waste heat of flue gas further for preheating condensate water.
The dust arrester for removing the particle in flue gas is also provided with at the end of described discharge duct, described dust arrester is deduster 16, described deduster 16, for removing ash content in flue gas, can adopt electrostatic precipitator 16 or sack cleaner 16 or other dust arresters in the present embodiment.The end of described deduster 16 also has the desulfurizer (not shown) for removing sulfur-bearing in flue gas.
Further, also comprise blower unit, described blower unit has air-vent and air-introduced machine 17, and described air-vent is communicated in the port of export of described discharge duct, and the exhaust outlet of described air-introduced machine 17 is communicated with chimney 18.Described economizer 14, low-pressure coal saver 15, deduster 16, desulfurizer and blower unit distribute successively along the flue gas discharge direction of described exhaust outlet, and.Described economizer 14, low-pressure coal saver 15, deduster 16, desulfurizer and blower unit are equipped with interval between in discharge duct flue gas discharge direction.
Further, also comprise storage slag bath 11, described storage slag bath 11 is connected to the slag-drip opening 10 of described burner hearth 12, and described storage slag bath 11 is vertically positioned at the below of the slag-drip opening 10 of described burner hearth 12.After solid refuse burning completely, remaining solid slag will be discharged by slag-drip opening 10.Described storage slag bath 11 is for depositing the solid slag after burning.
The efficient incinerating method of municipal refuse of the low corrosion that the utility model that the efficient CIU of municipal refuse of the low corrosion that the utility model relates in use relates to relates to, comprises the following steps:
1) pretreatment
By solid refuse (urban solid garbage) according to being whether that rubbish from cooking is classified, sorted rubbish from cooking entered installation for fermenting (fermentation vat 6) after entering the process such as high temperature sterilization and carries out anaerobic fermentation, the biogas that in installation for fermenting (fermentation vat 6), fermentation produces enters described preposition burner 5 and rearmounted burner 9 after removing moisture by dehydrating unit (dehumidifier 7), burns as fuel;
Non-rubbish from cooking is after removing the operations such as metal, and enter waste deposit room and carry out stacking process, stacking process effectively can be separated the superficial water of solid refuse, reaches the object of preliminarily dried.
2) mixed combustion
Solid refuse (non-rubbish from cooking) through stacking process is sent to into feed bin 1, under the acting in conjunction of shutoff damper 2 and batch plant 3, solid refuse is laid on above described fire grate 4 uniformly, after the preheating and drying of the First air that the solid refuse entering fire grate 4 enters through First air air outlet, heat convection and radiation heat transfer is carried out under the effect of preposition burner 5, the gasification that solid refuse can complete volatile matter faster and the process of catching fire, following solid refuse burns along with fire grate 4 enters central combustion district (fire grate 4 middle part), the higher solid refuse that can make of temperature herein carries out Thorough combustion, also the flame by incineration firing pushes fire grate 4 central authorities to, flame is assembled in fire grate 4 central authorities, form localized hyperthermia more than 850 DEG C, effectively can reduce the generation of bioxin,
Partially combusted solid refuse enters fire grate 4 afterbody (near the one end at slag-drip opening 10 place) and carries out last burning subsequently, and solid refuse completes burnout under the effect of rearmounted burner 9 herein; Due under the effect of preposition burner 5 and rearmounted burner 9, solid refuse is more concentrated at central combustion district flame, and ignition temperature becomes higher, effectively can reduce the generation of the contaminative compounds such as bioxin in combustion process.The waste residue of the solid refuse in afterburnt is expelled to storage slag bath 11 by described slag-drip opening 10.
In combustion, start described blower unit (air-introduced machine 17) and carry out described burner hearth 12 exhausting, promote the circulation of the flue gas in burner hearth 12, and then enter in discharge duct (boiler flue 13).The flue gas that the discharge duct (boiler flue 13) that the exhaust outlet of described burner hearth 12 is communicated with is discharged is successively by economizer 14 and low-pressure coal saver 15, economizer 14 carrys out heated feed water for the waste heat absorbing flue gas, and low-pressure coal saver 15 absorbs the waste heat of flue gas further for preheating condensate water.Be further advanced by described deduster 16 by the flue gas of economizer 14 and low-pressure coal saver 15 and remove solid particle wherein, by the flue gas after described deduster 16 again by sulfur-bearing in desulfurizer removing flue gas, the flue gas after desulfurizer is by discharging by chimney 18 after air-introduced machine 17.
In the process of mixed combustion, can regulate preposition burner 5 and rearmounted burner 9 according to characteristics such as the moisture content of the solid refuse through stacking process, volatile matter content and porositys; When moisture content height, increase the aperture of preposition burner 5, the methane quantity of burning in preposition burner 5 is increased, burning produces more heat, thus the moisture in solid refuse is gasified as early as possible, solid refuse catches fire as early as possible, also increases the aperture of rearmounted burner 9 simultaneously, makes completing smoothly of burnout; When the volatile matter content of solid refuse or porosity larger time, the aperture of preposition burner 5 and rearmounted burner 9 can be reduced, to save the use amount of biogas.
The efficient CIU of municipal refuse of the low corrosion that the utility model relates to, by the cooperation of steam generator system and the auxiliary combustion system of biogas, what be further advanced by described batch plant is designed for control inlet amount; The burner comprised by the auxiliary combustion system of described biogas, dehydrating unit and the cooperation for the installation for fermenting by rubbish from cooking fermentation process, the moisture content avoided due to the rubbish from cooking in solid refuse is the highest, need the time of stacking process long before burning, and need absorption heat that the phenomenon of the reduction of combustion chambers burn temperature can be caused to occur owing to participating in moisture vaporization in burning process; Simultaneously also by the main source that the salinities such as the NaCl avoided in rubbish from cooking are inorganic chlorines, HCl can be changed in combustion, thus cause the phenomenon of the corrosion failure of heating surface.
Rubbish from cooking is carried out fermentation process by the technical scheme used, and the inorganic chlorine of the overwhelming majority is all stayed in zymotic fluid with the form of salinity, reduces the introducing reducing chlorine source, thus reduce the chlorine corrosion of heating surface in source; Because described burner is connected to described combustion chamber, described burner, dehydrating unit are communicated with and the design of installation for fermenting serial communication successively, described fermentation vat is used for rubbish from cooking to carry out fermentation process, the biogas produced enters burner (preposition burner and rearmounted burner) and burns after dehydrating unit, more takes full advantage of the recovery effect of the energy.
By the design of fire grate, after solid refuse through stacking process is sent to combustion chamber, under the effect of batch plant, solid refuse is laid on above fire grate uniformly, the solid refuse entering fire grate, after the preheating and drying of First air, is convenient to carry out heat convection and radiation heat transfer under the effect of burner (preposition burner).
By the design that fire grate tilts toward described slag-drip opening direction, be convenient to solid refuse enter fire grate afterbody and carry out last burning, solid refuse completes burnout under the effect of burner (rearmounted burner) herein, be convenient on the one hand solid refuse under gravity automatically under slide to fire grate afterbody (near slag-drip opening), cost-saving; Also the abundant after-flame of fixed fuel is made on the other hand.
Enter the solid refuse of fire grate after the preheating and drying of First air, heat convection and radiation heat transfer is carried out under the effect of preposition burner, the gasification that solid refuse can complete volatile matter faster and the process of catching fire, following solid refuse burns along with fire grate enters central combustion district, the higher solid refuse that can make of temperature herein carries out Thorough combustion, solid refuse enters fire grate afterbody and carries out last burning subsequently, and solid refuse completes burnout under the effect of rearmounted burner herein; Due under the effect of preposition burner and rearmounted burner, solid refuse is more concentrated at central combustion district flame, and ignition temperature becomes higher, effectively can reduce the generation of the contaminative compounds such as bioxin in combustion process; In the process of mixed combustion, can regulate preposition burner and rearmounted burner according to characteristics such as the moisture content of the solid refuse through stacking process, volatile matter content and porositys; When moisture content height, increase the aperture of preposition burner, the methane quantity of burning in preposition burner is increased, burning produces more heat, thus the moisture in solid refuse is gasified as early as possible, solid refuse catches fire as early as possible, also increases the aperture of rearmounted burner simultaneously, makes completing smoothly of burnout; When the volatile matter content of solid refuse or porosity larger time, the aperture of preposition burner and rearmounted burner can be reduced, to save the use amount of biogas.
The efficient CIU of municipal refuse of the low corrosion that the utility model relates to, described economizer is positioned at boiler flue afterbody, carrys out heated feed water for the waste heat absorbing flue gas; Described low-pressure coal saver is positioned at boiler flue afterbody, position after economizer, for carrying out degree of depth recovery, for preheating condensate water to the waste heat of flue gas.
Described blower unit is positioned at the port of export (after deduster) of described discharge duct, and for increasing the fluid ability of flue gas, flue gas, by also needing further through process such as desulfurization after deduster, then enters chimney, enters in air.Secondary blast mouth is used for the required oxygen that burns completely that feeding secondary wind provides solid refuse.The heat that incineration firing produces is for heating the water in water-cooling wall; Inner Wall of Combustion Chamber is water screen tube, is full of recirculated water in water screen tube, and become steam after recirculated water heat absorption, steam does work after entering steam turbine, and drive steam turbine to rotate, steam turbine, at drive electrical generators rotary electrification, make use of resource fully.
The efficient incinerating method of municipal refuse of the low corrosion that the utility model relates to, equipment needed thereby is simple, equipment investment is few, and easy and simple to handle, realizes the operation of automation, in solid refuse combustion process, reduce the introducing reducing chlorine source, thus reduce the chlorine corrosion of many heating surfaces, ensure that the quick ignition of the solid refuse of combustion process, smooth combustion and complete after-flame, both ensure that the safety and stability Effec-tive Function of grate boiler, again reduce the generation of the pollution compounds such as bioxin.
The above embodiment only have expressed several embodiment of the present utility model, and it describes comparatively concrete and detailed, but therefore can not be interpreted as the restriction to the utility model the scope of the claims.It should be pointed out that for the person of ordinary skill of the art, without departing from the concept of the premise utility, can also make some distortion and improvement, these all belong to protection domain of the present utility model.Therefore, the protection domain of the utility model patent should be as the criterion with claims.
Claims (9)
1. the efficient CIU of the municipal refuse of low corrosion, is characterized in that, comprise
Steam generator system, described steam generator system comprises the combustion chamber with cavity, and described combustion chamber has charging aperture, slag-drip opening, air inlet and exhaust outlet;
The auxiliary combustion system of biogas, the auxiliary combustion system of described biogas comprises burner, dehydrating unit and for the installation for fermenting by rubbish from cooking fermentation process, described burner is connected to described combustion chamber, described burner, dehydrating unit and installation for fermenting serial communication successively.
2. the efficient CIU of the municipal refuse of low corrosion according to claim 1, is characterized in that, described combustion chamber has the fire grate for solid refuse of banking up, and described charging aperture is communicated in described fire grate;
Also comprise feeding device, described feeding device is communicated with described charging aperture, and described feeding device is arranged between described fire grate and charging aperture, and described fire grate is communicated in described feeding device.
3. the efficient CIU of the municipal refuse of low corrosion according to claim 2, it is characterized in that, described charging aperture, fire grate and slag-drip opening are arranged in order in the horizontal direction, and described charging aperture, fire grate and slag-drip opening are vertically in upper-lower position successively, the plane at described fire grate place tilts toward described slag-drip opening direction.
4. the efficient CIU of the municipal refuse of low corrosion according to claim 2, is characterized in that, described burner comprises preposition burner and rearmounted burner;
Described preposition burner is all communicated with described dehumidifier by gas pipeline with rearmounted burner, described preposition burner is arranged at the inwall of described combustion chamber near the side of charging aperture and toward described fire grate, and described rearmounted burner is arranged at the inwall of described combustion chamber near the side of slag-drip opening and toward described fire grate.
5. the efficient CIU of municipal refuse of the low corrosion according to claim 1-4 any one, it is characterized in that, also include feed bin and the shutoff damper for controlling feed rate, enter feed bin and be communicated in described charging aperture, described shutoff damper is movably connected on the opening and closing of described charging aperture for charging aperture.
6. the efficient CIU of municipal refuse of the low corrosion according to claim 1-4 any one, is characterized in that, the waste heat also comprised for absorbing flue gas comes economizer and the low-pressure coal saver of heated feed water;
Described exhaust outlet is communicated with discharge duct, and described economizer, low-pressure coal saver are set in turn in described discharge duct along the flue gas discharge direction of exhaust outlet, have interval along in discharge duct flue gas discharge direction between described economizer, low-pressure coal saver.
7. the efficient CIU of the municipal refuse of low corrosion according to claim 6, is characterized in that, also comprise blower unit, and described blower unit has air-vent and air-introduced machine, and described air-vent is communicated in the port of export of described discharge duct.
8. the efficient CIU of municipal refuse of the low corrosion according to claim 1-4 any one, is characterized in that, also comprise the Secondary Air air outlet for providing oxygen, described Secondary Air air outlet is communicated in described combustion chamber.
9. the efficient CIU of municipal refuse of the low corrosion according to claim 1-4 any one, is characterized in that, be provided with the water screen tube being full of recirculated water in described combustion chamber, described water screen tube is communicated with steam turbine, and described steam turbine is connected with generator.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201420590559.XU CN204114954U (en) | 2014-10-13 | 2014-10-13 | The efficient CIU of municipal refuse of low corrosion |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201420590559.XU CN204114954U (en) | 2014-10-13 | 2014-10-13 | The efficient CIU of municipal refuse of low corrosion |
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| CN204114954U true CN204114954U (en) | 2015-01-21 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105570898A (en) * | 2014-10-13 | 2016-05-11 | 广州特种承压设备检测研究院 | Low-corrosion and high-efficiency city garbage combusting system and method |
-
2014
- 2014-10-13 CN CN201420590559.XU patent/CN204114954U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105570898A (en) * | 2014-10-13 | 2016-05-11 | 广州特种承压设备检测研究院 | Low-corrosion and high-efficiency city garbage combusting system and method |
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