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CN102746903A - Large-scale domestic garbage dry distillation and gasification furnace without exhaust gas or dioxin emission - Google Patents

Large-scale domestic garbage dry distillation and gasification furnace without exhaust gas or dioxin emission Download PDF

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Publication number
CN102746903A
CN102746903A CN2012102420499A CN201210242049A CN102746903A CN 102746903 A CN102746903 A CN 102746903A CN 2012102420499 A CN2012102420499 A CN 2012102420499A CN 201210242049 A CN201210242049 A CN 201210242049A CN 102746903 A CN102746903 A CN 102746903A
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gas
rubbish
dry distillation
combustion
destructive distillation
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CN102746903B (en
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余式正
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Abstract

The invention relates to a domestic garbage dry distillation and gasification furnace. The domestic garbage dry distillation and gasification furnace is divided into a plurality of standard dry distillation treatment units, a large-scale domestic garbage dry distillation and gasification furnace is formed according to different treatment capability requirements, a standard dry distillation unit is a cubic furnace body, a garbage dry distillation section (23) and a drying section (21) are arranged above the cubic furnace body, the garbage is subjected to dry distillation when the garbage is in an anaerobic state, dry distillation coal gas and carbide residues are decomposed, carbides are combusted at a lower combustion layer (6) to generate high temperature, water vapor and air are used as gasification agents, CO2 (carbon dioxide) and water vapor generated by the combustion are reduced by carbides at a reducing layer (7) in the high temperature state, gasified coal gas is generated, and dioxin is not generated; the garbage at the garbage dry distillation section (23) is subjected to heating and dry distillation by the high-temperature gasified coal gas in the lifting process, the high-temperature gasified coal gas is continuously lifted, the garbage at the drying section is dried, organic matters in the garbage are converted into clean fuel gas, the dry distillation coal gas and the gasified coal gas are collected for utilization, and the large-scale domestic garbage dry distillation and gasification furnace without exhaust gas or dioxin emission is realized.

Description

A kind of large-scale, no waste gas is with the domestic refuse destructive distillation-vapourizing furnace of dioxin discharging
Technical field
The present invention relates to a kind of follow-on built-up type domestic refuse destructive distillation-vapourizing furnace; Through putting into the melting pot to the two stage type gas generating furnace structure; Improve its processing efficiency; And make it to be suitable for the mode of unit combination, and can be according to the needs of different treatment ability, be combined into and be used for the large-scale domestic refuse destructive distillation-vapourizing furnace of treating refuse.Technical field belongs to environmental protection and energy-saving and emission-reduction.
Background technology
The structure of well-known , dioxin is that one or two oxygen combine two by the substituted phenyl ring of chlorine, so its generation must possess two conditions: the one, the existence of chlorine is arranged; Another is that oxidizing reaction takes place.Composting can have chlorine to exist, and burning is an oxidizing reaction, so waste incineration just in time meets two conditions that produce dioxin, in view of the above it can be asserted that: waste incineration unavoidably can produce Dioxins; Waste incineration produces a large amount of waste gas simultaneously, is discharged in the air the Greenhouse effect of contaminate environment, the aggravation earth; Atmosphere and surrounding environment are produced serious influence, receive coming down hard upon of the masses.Simultaneously, waste incineration investment is big, and running cost is high, and maintenance cost is high, makes the government in general city hold and can't stand, promotes difficulty, causes many cities to form garbage-surrounded cities, leads to the rubbish crisis.
We adopt the domestic refuse retorting technique to handle domestic refuse, the generation that can stop dioxin fully in the past.Because destructive distillation is the decomposition reaction of solid organic matters under the secluding air state, even there is chlorine to exist, does not have oxygen, oxidizing reaction does not take place can not produce dioxin yet; And then burning carbide (or inflammable gas), then, can not produce dioxin because there is not the existence of chlorine yet.This technology is just in time basic identical with the production technique of two stage type gas generating furnace, but the small scale of producer gas generator can only be used for the processing of day processing 100 tons of following domestic refuses; This just can not adapt to the actual needs of garbage treatment; The actual needs of big city domestic rubbish disposal particularly, for example Shanghai daily output rubbish is 20000 tons, 18400 tons in Beijing daily output rubbish; So require refuse treatment plant to maximize, the waste incineration field of 3000 tons of day processing is being set about building in Beijing.
The object of the present invention is to provide a kind of theory that can fundamentally stop to produce dioxin according to us about the rubbish destructive distillation; Utilize the substruction of producer gas generator to transform, innovate; A kind of novel, high-level efficiency is provided and can adopts the unit combination mode; The difference of processing power as requested, the synthetic daily handling ability of respective sets is at the large-scale domestic refuse destructive distillation-vapourizing furnace of 100-1000 ton (more than reaching); Both realize the discharging of the no dioxin of refuse treatment, non-exhaust emission, and satisfied the domestic refuse destructive distillation-vapourizing furnace of demand of the maximization of refuse treatment plant.
Summary of the invention
The present invention transforms, innovates on the basis of two stage type gas generating furnace, provides a kind of and is divided into a plurality of standard destructive distillation processing units to domestic refuse destructive distillation-vapourizing furnace, according to the needs of different treatment ability, is combined into large-scale domestic refuse destructive distillation-vapourizing furnace; Standard destructive distillation processing unit makes the producer gas generator cylindrical furnace into cube, sealing body of heater, is convenient to a plurality of processing units of assembly unit, realizes maximizing; Standard destructive distillation processing unit top is provided with the retort section and the dryer section of rubbish; Utilize rubbish to be under the anaerobic state earlier the rubbish destructive distillation; Decomposite inflammable gas (being referred to as " dry distillation gas ") and carbide residue; Carbide below burning produce high temperature, make vaporized chemical with water vapor and air, the carbide under the condition of high temperature is the CO of burning generation 2And water vapour (H 2O) reduction generates semi-water gas (CO, H 2And N 2Deng, can be referred to as " gasification gas "), the pyritous gasification gas the heating of the rubbish of retort section, makes rubbish destructive distillation (decomposition reaction) in the process of rising, and gasification gas continues to rise, heats the rubbish of dryer section, dry; Collect dry distillation gas and utilize, thereby both realized that domestic rubbish disposal do not have dioxin discharging, non-exhaust emission with gasification gas, realize again maximization built-up type domestic refuse destructive distillation-vapourizing furnace.
The technical scheme that the present invention solves its technical problem is:
The technical scheme of technical solution problem of the present invention is: be divided into a plurality of standard destructive distillation processing units to domestic refuse destructive distillation-vapourizing furnace, and the difference of processing power as required, respective sets is synthesized large-scale domestic refuse destructive distillation-vapourizing furnace; Each standard treated unit adopts cube and sealed structure, is convenient to a plurality of standard treated stove of assembly unit simultaneously unit, forms large-scale domestic refuse destructive distillation-vapourizing furnace, as the pit kiln of steel mill, realizes that refuse treatment plant maximizes; Each standard treated unit is inner, the pipe core of original cylindrical producer gas generator, changes the middle comb of the row of putting in order, and becomes symmetric left and right sides two portions to the standard treated unit separation; In order to let rubbish effectively heat, the width of every part rubbish generally is advisable at 1-2 rice; The top is provided with the retort section and the dryer section of rubbish; Utilize rubbish to be under the anaerobic state earlier the rubbish destructive distillation; Decomposite dry distillation gas and carbide residue; Carbide below zone of combustion burning produce high temperature, make vaporized chemical with water vapor and air, the carbide under the reducing zone condition of high temperature is the CO of burning generation 2And water vapour (H 2O) reduction generates gasification gas (CO, H 2And N 2Deng), for the rubbish of rubbish retort section provides the heating heat, decompose by the rubbish destructive distillation in the process that rises for the pyritous gasification gas, rises to the drying garbage section again and make rubbish heating, oven dry; In addition; Because the ventilation property of rubbish and carbide is bad; The resistance that scorching hot gasification gas sees through carbide and waste layer rising is bigger; Cause directly to obtain to heat heat from gasification gas and can't make the abundant destructive distillation of rubbish, drying, and because gasification gas rise obstructed, wherein reducing gas CO, N 2Be detained, the carbide burning is just not vigorous, the combustionvelocity of slowing down carbide; Thereby reduce the efficient of refuse treatment, for this reason, handle the unitary retort section of stove in the standard destructive distillation; Specially around with middle the high-temperature fuel gas chamber is set, the inwall of high-temperature fuel gas chamber has ventilation hole, dry distillation gas is through these ventilation holes entering high-temperature fuel gas chamber; Mix, pool together with gasification gas; The high temperature (more than 600 ℃) that relies on combustion gas makes the tarry vapours in the dry distillation gas produce cracking, generates micromolecular combustion gas; Heat the rubbish that is clipped in the middle through radiation fully destructive distillation simultaneously; In dryer section the combustion gas ventpipe is set, guiding gas (comprising gasification gas and dry distillation gas) rises; The breathing area of high-temperature fuel gas chamber is bigger than combustion gas ventpipe, so combustion gas is long in the high-temperature fuel gas chamber residence time, and rubbish is by fully heating, destructive distillation; And flow velocity is low, and the flue dust that is mixed in the gasification gas also drops, and plays dust separating effect; High-temperature fuel gas rises to dryer section from the combustion gas ventpipe, makes rubbish heating, drying; The water vapor that drying garbage produces must leave as early as possible, otherwise rubbish just can not get into the destructive distillation state, influences the processing efficiency of rubbish, for this reason; The escape pipe of water vapor is set between two combustion gas ventpipes, also has logical steam vent, the water vapor that drying garbage produces gets into water vapor hole escape pipe through ventilating pit, and fast rise arrives furnace roof; Because water vapor is not detained, and can leave rubbish flash baking as early as possible; Get into retort section, carry out decomposition reaction, so processing efficiency improves; At last, collect dry distillation gas and gasification gas, can carry out various utilizations; Drying garbage has consumed a large amount of vaporization heat, and the water vapor of generation also is a useful resource, can be in order to being used as vaporized chemical.
The invention has the beneficial effects as follows:
1, do not produce Dioxins
Waste incineration unavoidably can produce Dioxins.Rubbish is first in following rubbish destructive distillation of secluding air state in destructive distillation-vapourizing furnace, because there is not oxygen just can not produce dioxin; And then the combustion carbide, do not have chlorine to exist and can not produce dioxin yet.This is that the rationale that does not produce dioxin is handled in the rubbish destructive distillation.In fact, because the organism in the rubbish all changes clean gas into, all collect and utilize, discharging does not have dioxin naturally.
2, do not have exhaust gas emission, do not have smokestack, do not pollute
Waste incineration per ton will produce the waste gas of 4000-7000 cubic meter, constitutes the severe contamination of air and having a strong impact on of weather.Particularly the high temperature of waste incineration generation generates NOx and SOx, and is more serious to the influence of environment.Utilize domestic refuse destructive distillation-vapourizing furnace treating refuse, waste gas CO 2Be taken as the utilization of resources, do not have exhaust gas emission, do not constitute pollution environment.
3, rubbish need not classification
Domestic refuse destructive distillation-vapourizing furnace treating refuse, rubbish need not classification.Waste incineration needs refuse classification in order to suppress the generation of dioxin.This needs broad masses' cooperation, and the whole people take action and carry out refuse classification from the source.But China does not carry out the custom of refuse classification; Also need carry out separate waste collection, classification transportation, classification processing, increase many inputs.
4, realize real waste reductionization
The past people have unilateral understanding for minimizing: think that waste incineration is fallen, " eyes cannot see " is exactly minimizing.In fact conservation of matter, we can not " burn rubbish not had ", but become waste gas; Volume is big, and damaging range is wide, refers to that the physical form of rubbish changes: eliminated depleted rubbish; Convert useful clean gas to, the waste reductionization that this is just real.
5, also use, realize unique resource utilization to waste gas
The refuse treatment combustion of organic matter produces a large amount of waste gas, in the present invention the CO in the waste gas 2Also be used as resource, be reduced into CO to it and recycle, this is unique garbage as resource utilization.
6, unit combination realizes that refuse treatment plant maximizes
The past waste incineration unavoidably can produce Dioxins, and many treatment of urban garbage reconnaissances are difficulty very, thus require to maximize, to satisfy the needs of refuse treatment.And grate furnace in the past can't be realized maximizing, and investment is big, and popularization is restricted.The present invention can get up the fixed grate unit combination according to actual needs, constitutes large-scale grate furnace, can satisfy metropolitan demand, helps to crack the rubbish crisis.
7, overcome the difficult problem that the refuse treatment investment is big, running cost is high, maintenance cost is high
Garbage incinerating system is complicated; Need spend substantial contribution to carry out waste gas pollution control and treatment, flying dust disposal during processing; Cause the investment of refuse treatment big, running cost is high, maintenance cost is high, the government burden in general city and small towns does not rise, and becomes the hang-up that perplexs governments at all levels.The utilization of domestic refuse biological fuel gas overcomes this difficult problem fully.
8, energy-saving and emission-reduction are remarkable especially, can carry out the carbon transaction
The past garbage loading embeading produces a large amount of greenhouse gases, mainly is methane, and its Greenhouse effect are also stronger 21 times than CO2.The whole world is in order to tackle climate warming, and United Nations repeatedly holds the energy-saving and emission-reduction meeting.The discharging of methane is avoided in domestic refuse destructive distillation-vapourizing furnace treating refuse fully; Simultaneously, clean gas can replace fire coal, saves CO again 2Discharging, can carry out carbon transaction (CDM), betray the carbon index, obtain abundant additional income.
9, clean gas can have multiple application
The recycling of waste incineration can only do cogeneration, and waste incineration and generating electricity at first needs a large amount of investments, and it is more much more than the power station investment of building a same power generation capacity to build a garbage incinerating power plant; Secondly, the inefficiency of waste incineration and generating electricity has great amount of heat to run away with waste gas; The efficient of waste heat boiler and steam turbine is low; The 3rd, day treatment scale is at the small-scale garbage incinerating power plant below 200 tons, and economic benefit is low, is difficult to recoup the investment, and is not suitable for building garbage incinerating power plant and has become common recognition; The 4th, garbage incinerating power plant is produced unstable, the online difficulty.The present invention converts rubbish into clean gas, can directly supply domestic gas, or provides Industrial Boiler to use; It is higher also to can be used for fuel gas generation efficient, higher than the efficient of waste incineration and generating electricity; More can be used for baking bricks, consume the inorganics in the rubbish simultaneously; Can also carry out synthetic.All these can obtain other income, and refuse treatment becomes profitable new forms of energy.
Description of drawings
Figure 1A is the structural representation of single standard destructive distillation processing unit;
Figure 1B is its side sectional view (MN analyses and observe).
Fig. 2 is the rubbish destructive distillation-vapourizing furnace grate furnace floor plan synoptic diagram that is made up, constituted large-scale non-exhaust emission by standard destructive distillation processing unit;
Among the figure: 1---pneumatic blower or general gas blower, 2---the water vapour ventpipe, 3---the air ventpipe, 4---the tuyere of air and water vapour; 5---fire grate, 6---zone of combustion, 7---reducing zone; 8---the carbide residue that destructive distillation stays, 9---compile the high-temperature fuel gas chamber of gasification gas and dry distillation gas, 10---left and right briquetting; 11---effuser, 12---left pusher hydro-cylinder, 13---left opening for feed; 14---left binder hydro-cylinder, 15---the air mixture air outlet, 16---right binder hydro-cylinder; 17---dry distillation gas and water vapor air outlet, 18---right opening for feed, 19---right pusher hydro-cylinder; 20---feed throat, 21---dryer section, 22---the combustion gas ventpipe; 23---retort section (comprising the carbide residue), 24---the carbide residue that the rubbish destructive distillation is residual, 25---ash bed; 26---ceramic thermal barrier layer, 27---ash bucket, 28---fire door; 29---the bilateral ceramic thermal barrier layer, 30---the escape pipe of water vapor, 31---dry distillation gas and gasification gas effuser; 32---water steams effuser, I---first standard destructive distillation processing unit, II---second standard is done unit; The 3rd standard destructive distillation processing unit of III, IV---the 4th standard destructive distillation processing unit, N---until N standard destructive distillation place
Figure BSA00000748487000052
Concrete examples of implementation
According to Fig. 1, follow-on built-up type domestic refuse destructive distillation-vapourizing furnace is to be combined by standard destructive distillation processing unit.Standard destructive distillation processing unit adopts cube and sealed structure, and inner in the standard treated unit, the fire-resistant heat insulating material liner is used in the inwall of stove (26) and (29), prevents that heat scatters and disappears; Middle combustion gas ventpipe (22) and high-temperature fuel gas chamber (9) the pipe core of cylindrical producer gas generator in the past changes the row of putting in order become symmetric left and right two portions to the standard treated unit separation; In order to let rubbish can fully be heated destructive distillation and drying, the width of every part rubbish (being the distance between the combustion gas ventpipe (22)) is advisable with 1-2 rice; Because handle to as if rubbish; With producer gas generator handle to as if coal the difference of essence is arranged; So must put into the melting pot feed system: rubbish gets into from two opening for feeds (13) and (18) on left and right both sides, pushes rubbish in the stove through left and right two pusher hydro-cylinders (12) and (19); Receive the extruding of pusher hydro-cylinder (12) and (19), it is closely airtight that rubbish becomes, and pusher hydro-cylinder (12) and (19) all do not push rubbish in the stove, keeps the rubbish shutoff feed throat (20) that a part compresses, and prevents gas leak; In order to prevent that stove rubbish from hardening, furnace roof is provided with binder hydro-cylinder (14) and (16), after rubbish is gone into stove, drives left and right briquetting (10) and depresses from above, even rubbish hardens, also can guarantee reliable blanking; Interior retort section (23), dryer section (21), reducing zone (7), zone of combustion (6) and the ash bed (25) that rubbish is set down from the top of stove; Utilize rubbish to pile up together, lack the effect of driveing of air and rubbish destructive distillation generation dry distillation gas, rubbish just is in the secluding air state, in this state earlier rubbish heating destructive distillation; Decomposite dry distillation gas and carbide residue (24); Carbide below zone of combustion (6) burning produce high temperature, make vaporized chemical with water vapor and air, the tuyere (4) through air and water vapour blasts below stove through fire grate (5); Contact, burn with the carbide of zone of combustion (6), produce high temperature; In the top of zone of combustion (6) is reducing zone (7), the CO that zone of combustion (6) burning produces 2Reduced by the carbide under the condition of high temperature at reducing zone (7) with the water vapour that rises, generate gasification gas: C+CO 2→ 2CO and C+H 2O → CO+H 2The gas pipe and the pipe core of original producer gas generator are transformed into the high-temperature fuel gas chamber (9) of compiling gasification gas and dry distillation gas around the destructive distillation layer; The inboard of high-temperature fuel gas chamber (9) has ventilation hole; Dry distillation gas can get into high-temperature fuel gas chamber (9) through these ventilation holes, because the temperature of high-temperature fuel gas chamber (9) very high (more than 600 ℃) makes the tarry vapours that contains in the dry distillation gas; At high temperature produce cracking, generate micromolecular combustion gas; Through radiation indirect heating rubbish, make the abundant destructive distillation of the garbage drying that is clipped in the middle on the other hand; Air mixture rises to dryer section (21), and high-temperature fuel gas chamber (9) are made combustion gas ventpipe (22) into, straight-through furnace roof, and the rubbish that makes dryer section mainly is to receive combustion gas ventpipe (22) radiation heating, oven dry except the dry distillation gas heat drying that receives the top decilitre; Between two combustion gas ventpipes, insert the escape pipe (30) of water vapor, the escape pipe of water vapor (30) also has vapor opening, and the water vapor that drying garbage produces arrives furnace roof rapidly through the escape pipe (30) of vapor opening entering water vapor; Water vapor is not detained and fast rise, and rubbish is able to rapid drying, improves refuse treatment efficient; The sectional area of the sectional area ratio dryer section combustion gas ventilation comb (22) of retort section (23) high-temperature fuel gas chamber (9) is much bigger, and the flow velocity of combustion gas is slow, and the flue dust that is mixed in the gasification gas is fallen, and plays dust separating effect; When the stove internal combustion was unbalanced, producer gas generator can only turn down combustion gas ventpipe (22) and reduce temperature of combustion, if adopt pneumatic blower here; The tuyere (4) of a plurality of air and water vapour can be set, and according to stove internal combustion situation, for example temperature of combustion is high; Add-on with regard to increasing water vapor reduces temperature of combustion, regulates the equilibrium of stove internal combustion temperature, owing to increase water vapor as vaporized chemical; Can reduce the amount of blasting of air, just reduce N remaining in the combustion gas 2Gas has increased H again 2Generation, also just improve the calorific value of combustion gas; Dry distillation gas and gasification gas mix, and collect from effuser (31) together and utilize, and be different with the epimere gas of producer gas generator; What collect from water vapor effuser (32) mainly is the water vapor that drying garbage produces, and wherein contains the small portion dry distillation gas, can be used as vaporized chemical and uses; Save softening water and the mass energy that produces water vapor, wherein contain the part combustion gas, also can improve temperature of combustion in the zone of combustion burning; Increase the add-on of water vapor, improve the calorific value of combustion gas.
According to Fig. 2, combine N standard destructive distillation processing unit, if each standard destructive distillation processing unit daily handling ability is 100 tons, daily handling ability just can reach N * 100 ton.Promptly, 10 standard destructive distillation processing units just can realize 1000 tons of day processing as long as combining.And if N standard destructive distillation processing unit combines, except initial two the unit, the intermediary unit can save the ceramic thermal barrier layer (26) of both sides.
If require bigger daily handling ability, can be by Fig. 2, be combined into two groups or three groups, just can realize that daily handling ability surpasses rubbish destructive distillation-vapourizing furnace of 1000 tons and realizes maximization easily.
The practicality of industry
The present invention is not only applicable to refuse treatment, is applicable to producer gas generator and stalk gasifier yet, even is used for converting non-grain physiological clock to clean gas, realizes the alternative new forms of energy of fossil energy.

Claims (11)

1. follow-on built-up type domestic refuse destructive distillation-vapourizing furnace, its technical characterictic is: be divided into a plurality of standard destructive distillation processing units to domestic refuse destructive distillation-vapourizing furnace, according to the needs of different treatment ability, be combined into large-scale domestic refuse destructive distillation-vapourizing furnace.
2. standard destructive distillation processing unit according to claim 1; Its technical characterictic is: put into the melting pot the original feed system of producer gas generator: rubbish gets into from two opening for feeds (13) and (18) on left and right both sides, pushes rubbish in the stove through left and right two pusher hydro-cylinders (12) and (19); Receive the extruding of pusher hydro-cylinder (12) and (19), it is closely airtight that rubbish becomes, and pusher hydro-cylinder (12) and (19) all do not push rubbish in the stove, keeps the rubbish shutoff feed throat (20) that a part compresses, and prevents gas leak.
3. standard destructive distillation processing unit according to claim 1, its technical characterictic is: make the producer gas generator cylindrical furnace into cube, sealing body of heater, be convenient to a plurality of processing units of assembly unit, realize maximizing; Center combustion gas ventpipe (22) and high-temperature fuel gas chamber (9) the pipe core of cylindrical producer gas generator changes the row of putting in order become symmetric left and right two portions to the standard treated unit separation; In order to let rubbish can fully be heated destructive distillation and drying, the width of every part rubbish (being the distance between the combustion gas ventpipe (22)) is advisable with 1-2 rice.
4. standard destructive distillation processing unit according to claim 1, its technical characterictic is: the retort section (23) and the dryer section (21) of rubbish are set, reducing zone (7), zone of combustion (6) and ash bed (25) from top to bottom; Utilize rubbish to pile up together, lack the effect of driveing of air and rubbish destructive distillation generation dry distillation gas; Rubbish just is in the secluding air state, earlier the rubbish destructive distillation, decomposites dry distillation gas and carbide residue; Because do not have oxygen, oxidizing reaction do not take place, so just can not produce dioxin; Make vaporized chemical with water vapor and air, the tuyere (4) through air and water vapour blasts from the stove below through fire grate (5), contacts, burns with the carbide of zone of combustion (6), because there is not the existence of chlorine also can not produce dioxin.
5. standard destructive distillation processing unit according to claim 1, its technical characterictic is: carbide produces high temperature in zone of combustion (6) burning, the CO that the carbide under the condition of high temperature produces burning 2And water vapour (H 2O) reduction generates gasification gas: C+CO 2→ 2CO and C+H2O → CO+H 2The pyritous gasification gas the heating of the rubbish of rubbish retort section (23), makes rubbish destructive distillation, decomposition in the process of rising, coal gas continues to rise, heats the rubbish of dryer section (21), dry.Collect dry distillation gas and gasification gas and utilize, thereby both realized domestic rubbish disposal non-exhaust emission, the discharging of no dioxin.
6. standard destructive distillation processing unit according to claim 1; Its technical characterictic is: the escape pipe (30) that between two combustion gas ventpipes, inserts water vapor; The escape pipe of water vapor (30) has vapor opening; The water vapor that drying garbage produces arrives furnace roof rapidly through the escape pipe (30) of vapor opening entering water vapor; Water vapor is not detained and fast rise, and rubbish is able to rapid drying, improves refuse treatment efficient.
7. standard destructive distillation processing unit according to claim 1; Its technical characterictic is: adopt pneumatic blower, the tuyere (4) of a plurality of air and water vapour is set, according to stove internal combustion situation; If the incendiary temperature is high; Just increase the add-on of water vapor, reduce temperature of combustion, regulate stove internal combustion temperature and reach balanced.Owing to increase water vapor as vaporized chemical, can reduce the amount of blasting of air, just reduce N remaining in the combustion gas 2Gas has increased H again 2Generation, improve the calorific value of combustion gas.
8. standard destructive distillation processing unit according to claim 1, its technical characterictic is: dry distillation gas and gasification gas are mixed, collect from effuser (31) together and utilize; To collect dry distillation gas different and only collect gasification gas, epimere gas with the hypomere gas of producer gas generator; What collect from water vapor effuser (32) mainly is the water vapor that drying garbage produces, and wherein contains the small portion dry distillation gas, uses as vaporized chemical with it; Save softening water and save the energy consumption that produces water vapor; Wherein contain the part combustion gas, also can improve temperature of combustion, will increase the add-on of water vapor for the control temperature of combustion in the zone of combustion burning; The minimizing air blasts tired, thereby reduces N 2Content increases H 2Content improves the calorific value of combustion gas.
9. feed system according to claim 2, its technical characterictic is: harden in order to prevent stove rubbish, furnace roof is provided with binder hydro-cylinder (14) and (16); After rubbish is gone into stove; Drive left and right briquetting (10) and depress,, also can guarantee reliable blanking even rubbish hardens from above.
10. combustion gas ventpipe according to claim 3 (22) and high-temperature fuel gas chamber (9); Its technical characterictic is: the inboard of high-temperature fuel gas chamber (9) has ventilation hole; Dry distillation gas can get into high-temperature fuel gas chamber (9) through these ventilation holes, because the temperature of high-temperature fuel gas chamber (9) very high (more than 600 ℃) makes the tarry vapours that contains in the dry distillation gas; At high temperature produce cracking, generate micromolecular combustion gas; Through radiation indirect heating rubbish, make the abundant destructive distillation of the garbage drying that is clipped in the middle on the other hand.
11. combustion gas ventpipe according to claim 3 (22) and high-temperature fuel gas chamber (9); Its technical characterictic is: air mixture rises to dryer section (21); High-temperature fuel gas chamber (9) is made combustion gas ventpipe (22) into; Straight-through furnace roof, the rubbish that makes dryer section mainly is to receive combustion gas ventpipe (22) radiation heating, oven dry except the dry distillation gas heat drying that receives the part rising; The sectional area of the sectional area ratio dryer section combustion gas ventpipe (22) of retort section (23) high-temperature fuel gas chamber (9) is much bigger, and the flow velocity of combustion gas is slow, and the flue dust that is mixed in the gasification gas is fallen, and plays the effect of depositing dust.
CN201210242049.9A 2012-07-13 2012-07-13 Large-scale domestic garbage dry distillation and gasification furnace without exhaust gas or dioxin emission Expired - Fee Related CN102746903B (en)

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CN103555373A (en) * 2013-07-31 2014-02-05 余式正 Garbage dry distillation-gasification furnace with no dioxin and waste gas emission
CN104099108A (en) * 2013-04-08 2014-10-15 廖树汉 Furnace for acquiring regenerated gasoline and diesel oil through separation via air exhauster after wood carbonization
CN104140851A (en) * 2014-08-12 2014-11-12 余式正 Vertical negative-pressure garbage destructive-distillation incinerator without emission of dioxin or waste gas
CN104449873A (en) * 2014-11-25 2015-03-25 新密市环新生活垃圾处理有限公司 Pyrolytic gas making technology of household garbage
CN105985812A (en) * 2015-03-03 2016-10-05 深圳市鑫旭源投资有限公司 Pyrolysis and gasified combustion system used in complete garbage disposal device
CN106940017A (en) * 2017-04-17 2017-07-11 山东大学 The system and method for coal-burning power plant's cooperated with consumer waste gasification
CN107723030A (en) * 2017-11-10 2018-02-23 马加德 A kind of solid waste gasification system and its gasification process
CN110440268A (en) * 2019-08-09 2019-11-12 陈景鹤 The oxygen barrier carbonization of house refuse low temperature pyrogenation and second-time burning integrated device
CN111140858A (en) * 2020-01-19 2020-05-12 云南净美环保科技有限公司 Small-size domestic waste burns burning furnace
CN112239677A (en) * 2019-07-16 2021-01-19 陈晓辉 Fixed bed coal gasifier, fixed bed coal gasification and coal gasification hydrogen production system and process method
CN114276838A (en) * 2021-12-28 2022-04-05 张文斌 Carbon-neutralization symmetric-structure fixed bed multi-section biomass gasification method
CN115143473A (en) * 2022-09-02 2022-10-04 臣功环境科技有限公司 High-temperature dry distillation carbonization incineration device for household garbage

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Publication number Priority date Publication date Assignee Title
CN104099108A (en) * 2013-04-08 2014-10-15 廖树汉 Furnace for acquiring regenerated gasoline and diesel oil through separation via air exhauster after wood carbonization
CN104099108B (en) * 2013-04-08 2017-02-15 廖树汉 Furnace for acquiring regenerated gasoline and diesel oil through separation via air exhauster after wood carbonization
CN103555373A (en) * 2013-07-31 2014-02-05 余式正 Garbage dry distillation-gasification furnace with no dioxin and waste gas emission
CN104140851B (en) * 2014-08-12 2017-10-31 余式正 It is a kind of Wu bioxin and the vertical negative-pressure rubbish dry-distillation incineration stove of non-exhaust emission
CN104140851A (en) * 2014-08-12 2014-11-12 余式正 Vertical negative-pressure garbage destructive-distillation incinerator without emission of dioxin or waste gas
CN104449873A (en) * 2014-11-25 2015-03-25 新密市环新生活垃圾处理有限公司 Pyrolytic gas making technology of household garbage
CN104449873B (en) * 2014-11-25 2017-06-06 江苏三色环境科技有限公司 A kind of domestic garbage pyrolysis gas-made technology
CN105985812A (en) * 2015-03-03 2016-10-05 深圳市鑫旭源投资有限公司 Pyrolysis and gasified combustion system used in complete garbage disposal device
CN106940017A (en) * 2017-04-17 2017-07-11 山东大学 The system and method for coal-burning power plant's cooperated with consumer waste gasification
CN107723030A (en) * 2017-11-10 2018-02-23 马加德 A kind of solid waste gasification system and its gasification process
CN107723030B (en) * 2017-11-10 2024-03-29 马加德 Solid waste gasification system and gasification method thereof
CN112239677A (en) * 2019-07-16 2021-01-19 陈晓辉 Fixed bed coal gasifier, fixed bed coal gasification and coal gasification hydrogen production system and process method
CN110440268A (en) * 2019-08-09 2019-11-12 陈景鹤 The oxygen barrier carbonization of house refuse low temperature pyrogenation and second-time burning integrated device
CN111140858A (en) * 2020-01-19 2020-05-12 云南净美环保科技有限公司 Small-size domestic waste burns burning furnace
CN114276838A (en) * 2021-12-28 2022-04-05 张文斌 Carbon-neutralization symmetric-structure fixed bed multi-section biomass gasification method
CN115143473A (en) * 2022-09-02 2022-10-04 臣功环境科技有限公司 High-temperature dry distillation carbonization incineration device for household garbage

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