CN1995821A - High-temperature air burning method for garbage and device therefor - Google Patents
High-temperature air burning method for garbage and device therefor Download PDFInfo
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- CN1995821A CN1995821A CN 200610123749 CN200610123749A CN1995821A CN 1995821 A CN1995821 A CN 1995821A CN 200610123749 CN200610123749 CN 200610123749 CN 200610123749 A CN200610123749 A CN 200610123749A CN 1995821 A CN1995821 A CN 1995821A
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Abstract
The invention discloses a sludge and high-temperature air incinerating method and the equipment, which comprises stoker furnace, burnout room and regenerative high temperature air generator. The regenerative high temperature air generator comprises the inlet of high-temperature smoke; left-right flues connected with the inlet of high-temperature smoke; the baffle of smoke inlet for controlling the circulation of flues at left-right sides, the baffle of air inlet; gear and rack transmission mechanism for adjusting the opening status of flues at two sides and air inlet; high-temperature plate regenerative body located in flues at left-right sides; four-way switch valve for controlling smoke and air, which enters into the high-temperature plate regenerative body; wind inlet pipe located at the back end of high-temperature plate regenerative body and wind outlet pipe located at the front end of high-temperature plate regenerative body. The invention is provided with compact structure, small occupied land, small investment, high treatment efficiency, lessening assistant fuel greatly, low operation cost, good environmental protection effect, and treating sludge with high water component quickly, expediently and safely. At the same time the environmental protection demand for sludge treatment is satisfied and it is provided with good applicable prospect.
Description
Technical field
The present invention relates to the high-efficiency low-pollution sludge incineration treatment system of the grate firing of high-temperature and low-oxygen combustion technology, be specifically related to sludge high temperature air incinerating method and device.
Background technology
Mud is the accessory substance that life and trade effluent are handled, this accessory substance is rich in microorganism, pathogen, virus etc., has stronger pollution character, if it is mishandling, can form pollution spread widely, the approach of its pollution has usually: the random stacking of (1) mud will be infiltrated surface soil layer polluted surface water system; (2) do not carry out the mud that hygienization handles and enter the farmland, may directly threaten human food chain; (3) mud distributes stench, or distributes harmful substance in atmosphere, atmosphere is formed pollute.The method of Treatment of Sludge mainly contains: (1) agriculture compost.But contain harmful substances such as a certain amount of heavy metal element and virus, pathogen, parasitic ovum in the mud, impose on the farmland and can produce toxic action to the mankind by the transmission of food chain and biological chain.(2) mud landfill.The mud burying method is simple, and expense is cheap, is a kind of main disposal options at some national landfill therefore, but landfill is occupied a large amount of soils, simultaneously, because mud contains certain noxious material, landfill is improper might be because of the leaching contaminated soil and the underground water of leachate.(3) mud is thrown the sea.Utilize the self-purification capacity of ocean, throw the sea and handle mud and adopted by many countries always, but since this disposal options to marine ecology, environmental sanitation and serious consequence that water pollution caused, this method is restricted gradually.(4) sludge incineration.Because burning process energy consumption height, the required energy of oxidation reaction can not be self-supporting, needs other makeup energy, so the operating cost height.But it is fast with processing speed, minimizing degree height, reusing of energy source, outstanding feature such as it is thorough to sterilize and being celebrated.
Countries in the world all more strict requirement has been proposed in time and the shared space that Treatment of Sludge spent, thereby the sludge incineration technology progressively becomes the mainstream technology of Treatment of Sludge, more and more is subjected to the favor of countries in the world.Burning process is except consumes energy, beyond cost and the running cost height, also can bring harmful substances such as smoke pollution and generation bioxin, at present, developed country is all in the discharge standard of formulating stricter solid incinerator flue gas, and this also will propose higher requirement to the burning of mud.
Sludge incineration is now handled usually with fluidized-bed combustion boiler and kiln, the mud that requires stove is through just handling, go into the stove sludge water content about 80%, need to add a large amount of auxiliary fuels, for UTILIZATION OF VESIDUAL HEAT IN waste heat boiler need be installed in addition, cause system complex, the operating cost height needs government to give double subsidy to Treatment of Sludge with the generating electricity price simultaneously and just can keep.So, the key of sludge incineration treatment process be to develop thermal efficiency height, expensive little, operating cost is low, and the burning process of compliance with environmental protection requirements.
Summary of the invention
The purpose of patent of the present invention is to overcome the shortcoming that prior art exists, and provides that a kind of investment is little, operating cost is low, the thermal efficiency is high, and the sludge high temperature air processor of compliance with environmental protection requirements, and this device can be handled the former primary sludge of 90% moisture; The input of auxiliary fuel is only in order to finish sludge incineration, and is not used in cogeneration, can significantly reduce the input amount of auxiliary fuel, reduces operating cost; Can directly absorb the heat storage of high-temperature high dust flue gas heat simultaneously by exploitation, amplitude peak reclaims the waste heat in the flue gas.
Another purpose of the present invention is to provide the method for sludge high temperature air burning.
Purpose of the present invention is achieved through the following technical solutions:
Sludge high temperature air incinerator, comprise the grate furnace that is connected with the bituminous coal charge pipe with the mud charge pipe, be positioned at the burning chamber of grate furnace top, also comprise the accumulation of heat typed high temperature air generator, described accumulation of heat typed high temperature air generator comprises high-temperature flue gas entry, the left and right sides flue that is communicated with high-temperature flue gas entry, the smoke inlet baffle plate of control left and right sides flue circulation, the air intake baffle plate, adjust the wheel and rack transmission mechanism of the opening of left and right sides flue and air intake, be positioned at the board-like heat storage of high temperature of left and right sides flue, passage behind the board-like heat storage of control high temperature is connected four-way switching valve with low temperature flue, be positioned at the blast pipe on the passage behind the board-like heat storage of high temperature and be positioned at the back discharge pipe of the board-like heat storage front end of high temperature; Described high-temperature flue gas entry is communicated with burning chamber, and low temperature flue is connected with sack cleaner; Blast pipe is connected with pressure fan, and discharge pipe is communicated with overfiren air port and bellows in the burning chamber respectively, sends into the high-temperature low-oxygen air.
Described smoke inlet baffle plate and air intake baffle plate are made by nonmetal temperature-resistant material, and there is the cooling layer on the surface, and the pulley of walking is arranged at the bottom, is driven by transmission mechanism.
Described wheel and rack transmission mechanism comprises gear, tooth bar, pulley and guide rail, realizes the pass with air register of opening of a side gas baffle, and the opening of the pass of opposite side gas baffle and air register.
Described grate furnace comprises propeller, multistage fixed grate, multistage primary air nozzle, bellows, dirt trap, lime stone spout, the alternate successively layout of described multistage fixed grate and multistage primary air nozzle, dirt trap is positioned at the bottom of grate furnace, No. one time bellows one end is communicated with discharge pipe, the other end is connected with multistage primary air nozzle respectively, the high-temperature low-oxygen air is sent into multistage primary air nozzle, and the lime stone spout is equipped with at grate furnace reducing chimney arch place, squirts sour gas such as limestone desulfurization in flue gas.
Described burning chamber comprises overfiren air port and furnace arch, furnace nose, and described overfiren air port is sent into the high-temperature low-oxygen air from discharge pipe, impels further burning; Described furnace arch, furnace nose is a triangle, and with the time of prolong smoke in burning chamber, and it is even to make flue gas enter the high-temperature flue air-flow.
Utilize said apparatus to carry out the method that the sludge high temperature air burns: mud and coal from mud charge pipe and bituminous coal charge pipe add in proportion, in the grate furnace internal combustion, not burning gas sends into the secondary burnt wind by overfiren air port and further burns, the high-temperature flue gas that produces enters the accumulation of heat typed high temperature air generator by high-temperature flue gas entry, high-temperature flue gas is through heat storage, enter low temperature flue by four-way switching valve after emitting heat, and pass through sack cleaner, discharge through air-introduced machine and chimney, in this process, the active carbon nozzle that is provided with by low temperature flue, to the heavy metal in the flue gas He bioxin adsorb, by the sack cleaner of afterbody, in dedusting, further heavy metal and bioxin are collected; Enter the accumulation of heat typed high temperature air generator by blast pipe sneak into the part low-temperature flue gas of air-introduced machine outlet from the cold air of pressure fan after, absorb the heat of heat storage, form the high-temperature low-oxygen air, be communicated with overfiren air port and bellows in the burning chamber respectively through discharge pipe, send the high-temperature low-oxygen air to grate furnace and burning chamber, promote sludge incineration.
Described grate furnace internal combustion is that mud and coal add in proportion, add in the interior the superiors of the stove fixed grate, absorb the dry slightly back of the interior radiations heat energy of stove and push next stage to by propeller, the next stage fire grate is provided with primary air nozzle, material is received a high-temperature flue gas radiation in the stove and a wind heat convection of high-temperature low-oxygen simultaneously, make that moisture is overflowed in a large number in the fuel, the part volatile matter of may overflowing simultaneously, through behind the certain hour, push to burn in the next stage fixed grate by propeller again, this one-level and later on the propeller of level be contained on air channel, adding cooling water all around cools off, guarantee the burning of fuel volatile matter and carbon residue, the lime-ash that has burnt is sent into the lime-ash device, and the top of grate furnace is a reducing chimney arch, to guarantee that temperature in the stove is about 1000 ℃, the lime stone spout is equipped with at reducing chimney arch place, squirts sour gas such as limestone desulfurization in flue gas, removal efficiency about 50%.
The present invention has following advantage and effect with respect to prior art:
(1) this high-efficiency low-pollution sludge incinerating system is a purpose with sludge incineration and Btu utilization, and the auxiliary fuel less investment has reduced the operating cost of Treatment of Sludge.The burnout rate of whole system fuel is more than 95%, the thermal efficiency about 80%.
(2) fixed grate combines with the high-temperature low-oxygen air, suitable mud high-moisture (mass fraction reaches 90%), the characteristics that combustible component is few, and the primary air flow inlet is concentrated and has been avoided the air port blockage problem;
(3) the accumulation of heat typed high temperature air generator directly adopt the many ashes of high temperature flue gases as thermal source, be heat storage medium with the nonmetal cordierite and the mullite composite material of big heat transfer coefficient, be equipped with the both sides regulating system of flue gas air, can produce high temperature air continuously.
(4) in normal temperature air, sneak into the cleaning low-temperature flue gas, obtain the air of high-temperature low-oxygen by the accumulation of heat typed high temperature air generator.
(5) whole sludge handling process is furnished with and squirts lime stone, active carbon in the flue gas, and sack cleaner is realized high-temperature and low-oxygen combustion, NO in the stove simultaneously
xProduce and lack, discharge index satisfies national requirements for environmental protection.
More than comprehensive, this method for sludge treatment and system have treatment effeciency height, advantage that environment protecting is good, can be used in the processing municipal sludge widely, and application prospect is wider.
Description of drawings
Fig. 1 is a high-efficiency low-pollution sludge incineration device of the present invention.
Fig. 2 is the structural representation of accumulation of heat typed high temperature air generator in the high-efficiency low-pollution sludge incinerating system shown in Figure 1.
Fig. 3 is the high-temperature flue gas of air preheater in Fig. 1 high-efficiency low-pollution sludge incinerating system shown in Figure 2 and the left view of air register;
Fig. 4 is the high-temperature flue gas of air preheater in Fig. 1 high-efficiency low-pollution sludge incinerating system shown in Figure 2 and the vertical view of air register.
The specific embodiment
The present invention is further detailed explanation below in conjunction with drawings and Examples, but the scope of protection of present invention is not limited to the scope of embodiment statement.
Fig. 1～Fig. 3 shows concrete structure of the present invention, as shown in Figure 1, sludge high temperature air incinerator of the present invention comprises equipment such as grate furnace 1, burning chamber 2, high-temperature flue 4, accumulation of heat typed high temperature air generator 5, low temperature flue 6, sack cleaner 7, pressure fan 4, air-introduced machine 8, chimney 9, mud charge pipe 10, bituminous coal charge pipe 11.
Described grate furnace 1 structure comprises propeller 1-1, fixed grate 1-2, primary air nozzle 1-3, bellows 1-4, a dirt trap 1-5, lime stone spout 1-6, and mud adds inlet 10, bituminous coal adds inlet 11, and external burning chamber 2.Described multistage fixed grate 1-2 and multistage primary air nozzle 1-3 are staggered alternately, dirt trap 1-5 is positioned at the bottom of grate furnace 1, No. one time bellows 1-4 one end is communicated with discharge pipe 4-6, the other end is connected with multistage primary air nozzle 1-3 respectively, the high-temperature low-oxygen air is sent into multistage primary air nozzle 1-3, lime stone spout 1-6 is equipped with at grate furnace 1 reducing chimney arch place, squirts lime stone to remove sour gas such as sulfur trioxide in flue gas.Mud and coal add in proportion, add among the interior fixed grate 1-2 of the superiors of stove, absorb the dry slightly back of the interior radiations heat energy of stove and push next stage to by propeller 1-1, the next stage fire grate is provided with primary air nozzle 1-2, material is subjected to an interior high-temperature flue gas radiation of stove and a wind heat convection of high-temperature low-oxygen simultaneously, make that moisture is overflowed in a large number in the fuel, the part volatile matter of may overflowing simultaneously, through behind the certain hour, push to burn in the next stage fixed grate by propeller again, this one-level and later on the propeller of level be contained on air channel, add cooling water all around and cool off.The course of work of level is identical later on, has guaranteed the burning of fuel volatile matter and carbon residue, and the lime-ash of all burnt is sent into lime-ash device 1-5.The top of grate furnace 1 is a reducing chimney arch, and about 1000 ℃, lime stone spout 1-5 is equipped with at reducing chimney arch place, squirts sour gas such as limestone desulfurization in flue gas, removal efficiency about 50% with the temperature in the assurance stove.
Comprise overfiren air port 2-1, furnace arch, furnace nose 2-2 in burning chamber's 2 structures.Grate fired furnace 2 outlet contains and does not necessarily burn gas, at this moment sends into the secondary burnt wind at overfiren air port 2-1 and further burns, and furnace arch, furnace nose 2-2 is a triangle, can the time of prolong smoke in burning chamber, and it is even to make flue gas enter the high-temperature flue air-flow simultaneously.
Accumulation of heat typed high temperature air generator 5 is key equipments of native system, its structure as depicted in figs. 1 and 2, comprise high-temperature flue gas entry 3, low-temperature flue gas outlet 6, left and right sides flue 3-1, smoke inlet baffle plate 5-4-1, air intake baffle plate 5-4-2, the board-like heat storage 5-1 of high temperature, cinder catcher 5-2, shown in four-way switching valve 5-6, soot blower 5-3, cement output tank 5-5, blast pipe 4-3, the discharge pipe 4-4.Accumulation of heat typed high temperature air generator 5 adopts both sides to arrange, enters the heat absorption of high-temperature flue gas heat release and Cryogenic air at interval.Position shown in Figure 3, accumulation of heat typed high temperature air generator 5 comprises high-temperature flue gas entry 6, the left and right sides flue 3-1 that is communicated with high-temperature flue gas entry, the smoke inlet baffle plate 5-4-1 of control left and right sides flue circulation, air intake baffle plate 5-4-2, adjust the gear 5-4-3 and the rack gear 5-4-4 of the opening of left and right sides flue 3-1 and air intake 5-4-1, be positioned at the board-like heat storage 5-1 of high temperature of left and right sides flue 3-1, control enters the four-way switching valve 5-6 of board-like heat storage flue gas of high temperature and air, be positioned at the blast pipe 6 and the discharge pipe 4-4 that is positioned at the board-like heat storage front end of high temperature of the board-like heat storage of high temperature rear end; Described high-temperature flue gas entry is communicated with burning chamber, and low temperature flue is connected with sack cleaner; Blast pipe is connected with pressure fan, and discharge pipe is communicated with overfiren air port and bellows in the burning chamber respectively, sends into the high-temperature low-oxygen air.High-temperature flue gas enters the heat storage 5-1 on right side by flue 3, enters low temperature flue 6 by four-way switching valve 5-6 after emitting heat.And an other side of while, the hypothermia and hypoxia air is entered by blast pipe 4-3, absorbs the heat of left side heat storage, forms the high-temperature low-oxygen air, and back discharge pipe 4-4 gets rid of.In next time, four-way switching valve 5-6 turns to, high-temperature flue gas baffle plate 5-4-1 and high temperature air baffle plate 5-4-2 are driven by the gear 5-4-3 and the tooth bar 5-4-4 of rack and pinion drive mechanism simultaneously, adjust the opening in left and right sides flue and air channel, realize again and again heat from high-temperature flue gas to the Cryogenic air transmission.
The structure of high-temperature flue gas baffle plate 5-4-1 and high temperature air baffle plate 5-4-2 is seen Fig. 2 and Fig. 3.Baffle plate is made by nonmetal temperature-resistant material, and there is the cooling layer on the surface, and the pulley of walking is arranged at the bottom, is driven by transmission mechanism.It comprises cooling air channel 5-4-1-1, the air inlet 5-4-1-2 of cooling duct, air outlet 5-4-1-3, the gear 5-4-3 of transmission mechanism and tooth bar 5-4-4, and pulley 5-4-1-4 and guide rail 5-4-1-5.The transmission mechanism of rack-and-pinion can be realized the pass with air register of opening of logical side gas baffle, and the opening of the pass of opposite side gas baffle and air register.
Air system comprises pressure fan 4, cool air inlet 4-1, low temperature clean smoke inlet 4-2, accumulation of heat typed high temperature air generator blast pipe 4-3, outlet high temperature airduct 4-4, secondary air channel 4-5, overfiren air port 2-1, an airduct 4-6, bellows 1-4, a primary air nozzle 1-3.Pressure fan 4 one ends are connected with low temperature clean smoke inlet 4-2 with cool air inlet 4-1, and the other end is connected with blast pipe 4-3, and outlet high temperature airduct 4-4 is communicated with secondary air channel 4-5 and an airduct 4-6 respectively, and secondary air channel 4-5 is communicated with overfiren air port 2-1; One time airduct 4-6 is connected with a bellows 1-4.Normal temperature air mixes with the low temperature clean flue gas forms the hypothermia and hypoxia air, send into accumulation of heat typed high temperature air generator 5 by blast pipe 4-3, the heat absorption back forms the high-temperature low-oxygen air and is drawn by high temperature airduct 4-4, a part is sent into burning chamber as secondary wind by secondary wind 4-5, overfiren air port 2-1, another part is sent into bellows 1-4 No. one time by an airduct 4-6, and it is combustion-supporting that grate furnace 1 is sent into by primary air nozzle 1-3 in the back.
The lime-ash of grate furnace 1, accumulation of heat typed high temperature air generator 5, deduster 7 is collected by lime-ash device 1-5, accumulation of heat typed high temperature air generator cement output tank 5-5, sack cleaner cement output tank 7-1 respectively, is used for landfill behind unified the curing or paves the way.
When utilizing apparatus of the present invention to carry out the burning of sludge high temperature air, mud and coal from mud charge pipe 10 and bituminous coal charge pipe 11 add in proportion, in grate furnace 1 internal combustion, not burning gas sends into the secondary burnt wind by overfiren air port 2-1 and further burns, the high-temperature flue gas that produces enters accumulation of heat typed high temperature air generator 5 by high-temperature flue gas entry 3, high-temperature flue gas is through heat storage 5-1, enter low temperature flue by four-way switching valve 5-6 after emitting heat, and pass through sack cleaner, discharge through air-introduced machine and chimney, in this process, the active carbon nozzle that is provided with by low temperature flue 6, to the heavy metal in the flue gas He bioxin adsorb, by the sack cleaner 7 of afterbody, in dedusting, further heavy metal and bioxin are collected; Sneak into the part low-temperature flue gas of air-introduced machine 8 outlets from the cold air of pressure fan 4 after, enter accumulation of heat typed high temperature air generator 5 by blast pipe 4-3, absorb the heat of heat storage, form the high-temperature low-oxygen air, be communicated with overfiren air port 2-1 and a bellows 1-4 in the burning chamber 2 respectively through discharge pipe 4-4, send the high-temperature low-oxygen air to grate furnace 1 and burning chamber 2, promote sludge incineration.
Claims (8)
1, sludge high temperature air incinerator, comprise the grate furnace that is connected with the bituminous coal charge pipe with the mud charge pipe, be positioned at the burning chamber of grate furnace top, it is characterized in that described sludge high temperature air incinerator also comprises the accumulation of heat typed high temperature air generator, described accumulation of heat typed high temperature air generator comprises high-temperature flue gas entry, the left and right sides flue that is communicated with high-temperature flue gas entry, the smoke inlet baffle plate of control left and right sides flue circulation, the air intake baffle plate, adjust the wheel and rack transmission mechanism of the opening of left and right sides flue and air intake, be positioned at the board-like heat storage of high temperature of left and right sides flue, control enters the four-way switching valve of board-like heat storage flue gas of high temperature and air, be positioned at the blast pipe and the discharge pipe that is positioned at the board-like heat storage front end of high temperature of the board-like heat storage of high temperature rear end; Described high-temperature flue gas entry is communicated with burning chamber, and low temperature flue is connected with sack cleaner; Blast pipe is connected with pressure fan, and discharge pipe is communicated with overfiren air port and bellows in the burning chamber respectively, sends into the high-temperature low-oxygen air.
2, sludge high temperature air incinerator according to claim 1, it is characterized in that described smoke inlet baffle plate and air intake baffle plate made by nonmetal temperature-resistant material, there is the cooling layer on the surface, and the pulley of walking is arranged at the bottom, is driven by the wheel and rack transmission mechanism.
3, according to claim 1 and 2 described sludge high temperature air incinerators, it is characterized in that described wheel and rack transmission mechanism comprises gear, tooth bar, pulley and guide rail, realize the pass with air register of opening of a side gas baffle, and the opening of the pass of opposite side gas baffle and air register.
4, sludge high temperature air incinerator according to claim 1, it is characterized in that described grate furnace comprises propeller, multistage fixed grate, multistage primary air nozzle, bellows, dirt trap, the lime stone spout, described multistage fixed grate and multistage primary air nozzle are staggered alternately, dirt trap is positioned at the bottom of grate furnace, No. one time bellows one end is communicated with discharge pipe, the other end is connected with multistage primary air nozzle respectively, the high-temperature low-oxygen air is sent into multistage primary air nozzle, the lime stone spout is equipped with at grate furnace reducing chimney arch place, squirts lime stone to remove sour gas such as sulfur trioxide in flue gas.
5, sludge high temperature air incinerator according to claim 1 is characterized in that described burning chamber comprises overfiren air port and furnace arch, furnace nose, and described overfiren air port is sent into the high-temperature low-oxygen air of discharge pipe after the High-temperature Air Generator, impels further burning; Described furnace arch, furnace nose is a triangle, and with the time of staying of prolong smoke in burning chamber, and it is even to make flue gas enter the high-temperature flue air-flow.
6, sludge high temperature air incinerator according to claim 1 is characterized in that its heat storage of described accumulation of heat typed high temperature air generator adopts the thin plate heat-storing material, arranges along array structure, and soot blower is housed above, and cinder catcher and cement output tank are arranged below.
7, utilize the described device of claim 1～6 to carry out the method that the sludge high temperature air burns, it is characterized in that, utilize said apparatus to carry out the method that the sludge high temperature air burns: mud and coal from mud charge pipe and bituminous coal charge pipe add in proportion, in the grate furnace internal combustion, not burning gas sends into the secondary burnt wind by overfiren air port and further burns, the high-temperature flue gas that produces enters the accumulation of heat typed high temperature air generator by high-temperature flue gas entry, high-temperature flue gas is through heat storage, enter low temperature flue by four-way switching valve after emitting heat, and pass through sack cleaner, discharge through air-introduced machine and chimney, in this process, the active carbon nozzle that is provided with by low temperature flue, to the heavy metal in the flue gas He bioxin adsorb, by the sack cleaner of afterbody, in dedusting, further heavy metal and bioxin are collected; After sneaking into air-introduced machine exit portion low-temperature flue gas from the cold air of pressure fan, enter the accumulation of heat typed high temperature air generator by blast pipe, absorb the heat of heat storage, form the high-temperature low-oxygen air, be communicated with overfiren air port and bellows in the burning chamber respectively through discharge pipe, send the high-temperature low-oxygen air to grate furnace and burning chamber, promote sludge incineration.
8, method according to the described sludge high temperature air burning of claim 7, it is characterized in that described grate furnace internal combustion is that mud and coal add in proportion, add in the interior the superiors of the stove fixed grate, absorb the dry slightly back of the interior radiations heat energy of stove and push next stage to by propeller, the next stage fire grate is provided with primary air nozzle, material is received a high-temperature flue gas radiation in the stove and a wind heat convection of high-temperature low-oxygen simultaneously, make that moisture is overflowed in a large number in the fuel, the part volatile matter of may overflowing simultaneously, through behind the certain hour, push to burn on the next stage fixed grate by propeller again, this one-level and later on the propeller of level be contained on air channel, adding cooling jacket all around cools off, fuel volatile matter and the carbon residue remaining lime-ash that burnt is sent into the lime-ash device, the top of grate furnace is a reducing chimney arch, and the lime stone spout is equipped with at reducing chimney arch place, squirts lime stone to remove sour gas such as sulfur trioxide in flue gas.
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| Application Number | Priority Date | Filing Date | Title |
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| CNB2006101237490A CN100464121C (en) | 2006-11-24 | 2006-11-24 | High-temperature air burning method for garbage and device therefor |
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| CNB2006101237490A CN100464121C (en) | 2006-11-24 | 2006-11-24 | High-temperature air burning method for garbage and device therefor |
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| CN1995821A true CN1995821A (en) | 2007-07-11 |
| CN100464121C CN100464121C (en) | 2009-02-25 |
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| CN101694299A (en) * | 2009-10-21 | 2010-04-14 | 吴跃平 | Method for eliminating sludge through combustion |
| CN102297442A (en) * | 2011-07-21 | 2011-12-28 | 中能兴科（北京）节能科技股份有限公司 | Heat accumulating type temperature-reducing and dust-removing system and method |
| CN101598504B (en) * | 2009-07-03 | 2012-07-04 | 霍镰泉 | Method and device for controlling waste heat recovery system of kiln |
| CN103017173A (en) * | 2012-12-14 | 2013-04-03 | 高玉宗 | Garbage incinerator for utilizing waste heat of industrial hot air discharge pipeline |
| CN103939917A (en) * | 2014-04-03 | 2014-07-23 | 山东威澳环保科技有限公司 | Combustion intensifying device in furnace |
| CN104949128A (en) * | 2014-09-10 | 2015-09-30 | 方向 | Solid waste processing method |
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| CN1050414C (en) * | 1992-09-18 | 2000-03-15 | 黄哲元 | Multifunction crematory furnace |
| JP2001241623A (en) * | 2000-02-28 | 2001-09-07 | ▲将▼ ▲高▼野 | Burning method and device of waste containing waste plastic |
| CN2563442Y (en) * | 2002-07-23 | 2003-07-30 | 洪文虎 | Waste material incinerator |
| CN2634307Y (en) * | 2003-06-27 | 2004-08-18 | 清华大学 | Multistage incineration equipment of rotary kiln garbage gasifying and carbon ash cosmelting |
| JP4194983B2 (en) * | 2004-07-21 | 2008-12-10 | 株式会社荏原製作所 | Waste disposal method |
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| CN101598504B (en) * | 2009-07-03 | 2012-07-04 | 霍镰泉 | Method and device for controlling waste heat recovery system of kiln |
| CN101694299A (en) * | 2009-10-21 | 2010-04-14 | 吴跃平 | Method for eliminating sludge through combustion |
| CN102297442A (en) * | 2011-07-21 | 2011-12-28 | 中能兴科（北京）节能科技股份有限公司 | Heat accumulating type temperature-reducing and dust-removing system and method |
| CN103017173A (en) * | 2012-12-14 | 2013-04-03 | 高玉宗 | Garbage incinerator for utilizing waste heat of industrial hot air discharge pipeline |
| CN103017173B (en) * | 2012-12-14 | 2015-08-05 | 高玉宗 | A kind of incinerator utilizing industrial warm air discharge tubes road waste heat |
| CN105814175A (en) * | 2013-12-13 | 2016-07-27 | 株式会社Ihi | Tar reforming furnace |
| CN105814175B (en) * | 2013-12-13 | 2019-02-15 | 株式会社 Ihi | Modified by tar furnace |
| CN103939917A (en) * | 2014-04-03 | 2014-07-23 | 山东威澳环保科技有限公司 | Combustion intensifying device in furnace |
| CN103939917B (en) * | 2014-04-03 | 2016-03-23 | 山东威澳环保科技有限公司 | Intensified burning apparatus in a kind of stove |
| CN104949128A (en) * | 2014-09-10 | 2015-09-30 | 方向 | Solid waste processing method |
| CN110982554A (en) * | 2019-12-25 | 2020-04-10 | 中国成达工程有限公司 | System for treating tail gas containing acetylene carbide slag in process of producing acetylene by calcium carbide dry method |
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