CN202543162U - Device for pyrolyzing urban garbage for generating fuel oil - Google Patents
Device for pyrolyzing urban garbage for generating fuel oil Download PDFInfo
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- CN202543162U CN202543162U CN2012201708729U CN201220170872U CN202543162U CN 202543162 U CN202543162 U CN 202543162U CN 2012201708729 U CN2012201708729 U CN 2012201708729U CN 201220170872 U CN201220170872 U CN 201220170872U CN 202543162 U CN202543162 U CN 202543162U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
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- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
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Abstract
The utility model discloses a device for pyrolyzing urban garbage for generating fuel oil. The device comprises a garbage cabin, a scraper conveyor, a bag-breaking roller screen, a first belt conveyer, a first garbage roller screen, a sorting breaker, a second belt conveyer, a magnetic separator, a second garbage roller screen, a third belt conveyer, a semi-wet crushing mill, a fourth belt conveyer, a drier, a stirring mixer, a fifth belt conveyer, an extrusion molding machine and a pyrolytic reaction device. All the parts are mutually connected in turn. By using the device, the fuel oil which is easy to store and remotely convey is directly obtained from the garbage; the scope of application is wide; the mass and the volume of the urban garbage are obviously reduced through a garbage pretreatment technology; the pyrolyzing treating operation is high in elasticity and is strong in adaptability to the fluctuation of garbage components; less dust of smoke is generated from the pyrolyzing treatment for the urban garbage and the pyrolyzing treatment is almost free from secondary pollution; the pyrolyzing process is simple and is easy to operate and control; and the investment and running costs are low.
Description
Technical field
The utility model relates to a kind of domestic waste pyrolysis fuel oil equipment.
Background technology
Domestic waste is one of three major types solid waste, and it derives from refuse that daily routines human and animal produce in the city or the Litter that does not re-use.Like the residue in kitchen, the paper product that abandon, the electronic product of scrapping, the wrapping material of commodity etc., along with the development of urbanization process is rapid, the domestic waste generation also increases rapidly, according to statistics annual more than 100 hundred million tons of the solid waste that increase newly in the whole world in 2010.In the face of the severe situation that domestic waste produces, its treatment technology, the developed country such as the U.S. are just being made great efforts to explore in the whole world; Canada, Japan, Germany; The proposition early of states such as France through comprehensive treating process, realizes waste reductionization on the categorised collection basis of realizing rubbish, innoxious; The thinking of resource utilization, and set up quite complete separate waste collection system for handling.Make a general survey of global developed country and China's garbage treatment state of the art, see table 1, can find, mainly take at present to burn landfill, 3 kinds of comparatively common processing modes of compost.
Table 1 world major country process for treating urban garbage
| Country | Landfill % | Burn % | Compost % |
| The U.S. | 75 | 10 | 5 |
| France | 40 | 38 | 22 |
| Holland | 45 | 51 | 4 |
| Germany | 65 | 32 | 3 |
| Austria | 59.8 | 16.2 | 24 |
| Sweden | 35 | 55 | 10 |
| China | 92 | 3 | 5 |
From table 1, can find out, China, the U.S. and part European countries landfill disposal are still occupied bigger ratio, but compost, burning disposal has also occupied certain ratio.
1. landfill: landfill be organic composition in the domestic waste under the anaerobic condition of landfill yard, the process of decomposing through anaerobion.It is simple that landfill disposal has technology, and cost is lower, extremely wide to the adaptation of rubbish, need not carry out advantages such as sorting to rubbish; At present, landfill is the main method of garbage treatment.Although it is simple to operate that the garbage loading embeading processing has, cost is low, adapts to extremely wide advantage, simultaneously secondary pollution is arranged also, and occupies a large amount of land resources.
2. compost: the producing fertilizer from refuse in daily life treating processes is exactly to rely on the bacterium that extensively distributes voluntarily; Actinomycetes; Mikrobes such as fungi; Under certain artificial condition, controlledly promote and its essence is a kind of fermenting process by the organism of verivate degraded to the Biochemical processes that stable detritus transforms.The biologic garbage composting technology has realized the recovery of resource, has reached the requirement of technology of garbage disposal resource utilization, has promoted the benign cycle of nature material, and its volume generally is the 50%-70% of original volume after the employing compost treatment.For landfill,, when solving refuse treatment, realized the resource utilization target although compost is a kind of ecological technology of garbage disposal that requires that meets most.But it is big that the compost treatment technology exists facility investment, long processing period, and treatment capacity is little, and because some heavy metal can accumulate in soil, makes that the heavy metal content in the soil obviously improves, the problem of serious threat food chain.
3. burn: burning is a kind of domestic waste to be carried out the chemically treated technology of elevated temperature heat.As burning in the solid fuel input incinerator equipment, flammable composition and airborne oxygen in the domestic refuse carry out violent chemical reaction, discharge heat and high-temperature combustible gas body and a spot of solid lime-ash with domestic refuse.The high-temperature combustible gas body that incineration firing produces can be used as energy generating and utilizes.Through burning disposal, decompose, destroyed being harmful in the rubbish, toxic waste and various stench, utterly destroyed bacterium, virus, burning disposal can make rubbish loss of weight 70%-75%, decrement 80%-92%.But often contain obnoxious flavour such as SO in the combustion tail gas that discharges in the burning disposal process
2, HCl, NO
X, CO and dioxin-like chemical (PCOD
S/ PCDF
S) etc., the lime-ash of discharging contains a large amount of heavy metals and dioxin-like chemical etc. especially therein, if deal with improperly, all will produce secondary pollution, and therefore, discharging how to control noxious just becomes the key of consumer waste incineration.
Along with the progress of society and the renewal of idea, the raising of the development of urban economy and resident living level, the domestic waste day output increases considerably, and the proportion of combustiblesubstance is also increasing in the rubbish composition.How to handle these total amounts in hundred million tons, produce continually, the domestic refuse of serious environment pollution has become one of major issue of countries in the world city management.At present the waste disposal method that extensively adopts of countries in the world is sanitary landfill, and compost burns these three kinds of technology and all exists innoxious not thoroughly, and the resource utilization degree is low, and running cost is high, can't suppress to burn the dioxin-like chemical (PCOD that brings
S/ PCDF
S) discharge, the sour gas discharging, the heavy metal volatilization is shifted and the enrichment secondary pollution problems.Therefore, countries in the world are just striving to find more advanced domestic rubbish disposal technology.Refuse gasification generating and gasification and melting incineration technology are a new generation's technology of developing at present.Characteristics such as but because the domestic waste calorific value is low, water cut is high, and combustiblematerials is few make this binomial technical economic benefit poor, the industrial applications difficulty.
The master data of domestic waste is at present:
The average combustion heat value of composting: rubbish wet basis low value thermal value is 800-1000 card/kilogram
Msw water content 40-60%, unit weight are 0.4 kg/liter
Organic content in the rubbish: about 62%
According to above-mentioned data,, in the pyrolytic gasification process, need to absorb a large amount of heats if adopt the refuse pyrolysis gasification technology; And synthetic gas is with water vapor and combustible gas and deposit, therefore, and the synthetic gas calorific value that refuse gasification obtains lower (being generally 4-6MJ/Nm3); Be used to generate electricity its generating efficiency at 10-15%; Deficiency in economic performance can only be used for resident's heating, supply energy sources such as cooking air feed.And gasification and melting incineration is technological owing to its fusion in reactor drum, and temperature is more than 1300 ℃.The refuse gasification burning does not reach high like this temperature, needs extra other fuel that replenishes, and causes economic benefit low.
Summary of the invention
In order to overcome innoxious not thorough that prior art exists, the resource utilization degree is low, and running cost is high, can't suppress to burn the dioxin-like chemical (PCOD that brings
S/ PCDF
S) discharge; The sour gas discharging; Heavy metal volatilization is shifted and problems such as enrichment secondary pollution, economic benefit be low, and the utility model provides a kind of low heat value that can make, high-moisture; The domestic waste that combustiblematerials is few is utilized more fully, makes the domestic waste pyrolysis fuel oil equipment of its maximization of economic benefit.
The technical scheme that the utility model adopts is:
Domestic waste pyrolysis fuel oil equipment; It is characterized in that: comprise trash repository, scraper conveyor, broken bag trommel screen, first rotary conveyor, the first rubbish trommel screen, letter sorting crusher, second rotary conveyor, magnetic separator, the second rubbish trommel screen, the 3rd rotary conveyor, half wet crushing mill, the 4th rotary conveyor, drying machine, stirring mixer, the 5th rotary conveyor, single-lead-screw extruding briquetting machine and pyrolytic reaction equipment; The outlet of said trash repository is connected with the import of said scraper conveyor; The outlet of said scraper conveyor is connected with the import of said broken bag trommel screen; The outlet of said broken bag trommel screen is connected with the import of said first rotary conveyor; The outlet of said first rotary conveyor is connected with the import of the said first rubbish trommel screen; The import of the said letter sorting crusher of the outlet of the said first rubbish trommel screen links to each other, and the outlet of said letter sorting crusher links to each other with the said second rotary conveyor import, and the outlet of said second rotary conveyor links to each other with the import of said magnetic separator; The outlet of said magnetic separator links to each other with the import of the said second rubbish trommel screen; The outlet of the said second rubbish trommel screen links to each other with the import of said the 3rd rotary conveyor, and the outlet of said the 3rd rotary conveyor links to each other with the import of said half wet crushing mill, and the outlet of said half wet crushing mill links to each other with the import of said the 4th rotary conveyor; The outlet of said the 4th rotary conveyor links to each other with the import of said drying machine; The outlet of said drying machine links to each other with the import of stirring mixer, and the outlet of said stirring mixer links to each other with the import of said the 5th rotary conveyor, and the outlet of said the 5th rotary conveyor links to each other with the import of said single-lead-screw extruding briquetting machine; The outlet of said single-lead-screw extruding briquetting machine links to each other with the import of said pyrolytic reaction equipment, and the outlet of said pyrolytic reaction equipment links to each other with the import of said moisture eliminator.
Further; Described pyrolytic reaction equipment comprises burner, first cyclonic separator, pyrolysis reactor, second cyclonic separator and condensing surface; The import of described pyrolysis reactor links to each other with the outlet of described single-lead-screw extruding briquetting machine; The outlet of said pyrolysis reactor links to each other with the import of said second cyclonic separator; The outlet of said second cyclonic separator links to each other with the import of said condensing surface through blower fan, and the outlet of said condensing surface links to each other with said pyrolysis reactor through blower fan, and the bottom of said pyrolysis reactor links to each other with said burner; The top of said burner links to each other with the import of said first cyclonic separator, and the outlet of said first cyclonic separator links to each other with the import of said moisture eliminator through blower fan.
Further; Between described single-lead-screw extruding briquetting machine and described pyrolysis reactor, also be provided with lift, temporary storing bin and screw feeder; The outlet of described single-lead-screw extruding briquetting machine links to each other with the import of described lift; The outlet of described lift links to each other with the import of described temporary storing bin, and the outlet of described temporary storing bin links to each other with the import of described screw feeder, and the outlet of described screw feeder links to each other with the import of described pyrolysis reactor.
Further, the bottom of said burner is provided with blower fan.
Further; The lower end side of said pyrolysis reactor also is provided with screw feeder and feed bin; One end of said screw feeder links to each other with said pyrolysis reactor; The other end is connected with said feed bin, and the thermal barrier in the said feed bin gets into through said screw feeder and replenishes the thermal barrier that wears away in the said pyrolysis reactor.
Further, between said moisture eliminator and said stirring mixer, be provided with electronic belt scale.
Further, the bottom of said condensing surface is provided with basin.
Further, described half wet crushing mill comprises pulverizing topworks, casing, frame and drive unit; Described drying machine is the direct heating cocurrent drier, is provided with flight in the machine and conducts heat to guarantee the direct uniform contact of granulated garbage and flue gas; Said single-lead-screw extruding briquetting machine is the built-up type Squeezinggranulator, by homogeneous, stirs, and combinations such as extrusion molding, the homogeneous mixing part is made up of twin shaft blade and casing, and the extrusion molding part is made up of reducing Variable pitch screw, discharging orifice plate and housing.
Two common difficulties that the utility model is run into the development of various countries, the world today---rubbish surplus and energy deficiency are organically coordinated.Its technological core is an integrated technique: the first step is with the domestic refuse pre-treatment, processes calorific value at 15-20MJ/Nm
3, water cut＜10%, the ingredient stability garbage raw material particle of ash content＜8%; Second step was that this granulated garbage is processed calorific value through fast pyrogenation is 15-18MJ/Nm
3Biofuel oil.This oil can directly use in industry, substitutes many boilers, mover and the used fuel oil of turbine; But also can therefrom extract a series of chemical substances, like foodstuff additive, resin, medicament etc.Because what generate is liquid fuel, so can store at an easy rate and transport, not limited by the region.
When the utility model uses, utilize the driving grab bucket from trash repository, to take out raw material rubbish, deliver in the receiving hopper of refuse treatment production line, and deliver to brokenly rubbish in the bag trommel screen equably through scraper conveyor.Deliver to rubbish from cooking in the first rubbish trommel screen with first rotary conveyor as screen underflow less than the organism and the inorganics dirt of sieve aperture; Broken delivering to greater than the screen overflow of sieve aperture in the letter sorting crusher.Rubbish after fragmentation is sent in the magnetic separator with second rotary conveyor and further metal object is sorted out; Further screen underflow is got in the second rubbish trommel screen then and sort.Less than the inorganics dirt of sieve aperture as the building materials raw material; Screen overflow rubbish is sent into the 3rd rotary conveyor and is carried out the secondary pulverizing in rubbish half wet crushing mill.The advantage that secondary is pulverized is can moisture about 40% rubbish be pulverized, and extracts the rubbish of granularity＜20mm after the pulverizing.Rubbish after secondary is pulverized gets in the rotary shelf drier through the 4th rotary conveyor and carries out drying.After the belted electronic balance metering, send in the continuously stirring mixing machine through dried garbage raw material (moisture＜12%), simultaneously, additives such as CaO also mix in the adding stirring mixer after the belted electronic balance metering from feed bin together again.Garbage raw material behind the uniform mixing is sent into by the 5th rotary conveyor and is carried out homogeneous in the single-lead-screw extruding briquetting machine, stirs extrusion molding.Send into the temporary storing bin with chapelet from the garbage raw material particle (diameter＜Φ 15mm) that single-lead-screw extruding briquetting machine comes out, evenly send in the pyrolysis reactor through screw feeder again.The garbage gas that the pyrolysis reactor handle comes from condensing surface is as fluidizing medium.Get into the interior granulated garbage of pyrolysis reactor and mix, and under fluidised situation, conduct heat with the thermal barrier that comes from burner, mass transfer, and be heated rapidly to 800 ℃, and pyrolysis rapidly; Oil gas after pyrolysis gets into the ash content of isolating second cyclonic separator in the oil gas from the top exit of pyrolysis reactor; The oil gas of sloughing ash content is sent in the condensing surface cooling fast through blower fan and is obtained liquid fuel oil and put into basin and store.And the combustion gas that few part is not liquefied is sent in the pyrolysis reactor as fluidization gas through blower fan.The semicoke and the thermal barrier that come out from the pyrolysis reactor bottom get into the burner.Semicoke burns in burner provides thermal source, and the temperature of thermal barrier is heated to about 1000 ℃.Flue gas and thermal barrier are discharged through the top of burner and are got in first cyclonic separator, thermal barrier with get in the pyrolysis reactor again after flue gas separates, and flue gas is admitted to the drying machine garbage drying through blower fan.Wherein the thermal barrier in the feed bin gets into through screw feeder and replenishes the thermal barrier that wears away in the pyrolysis reactor.
The utility model is directly produced oil fuel through with the rubbish pre-treatment from rubbish, it is higher that its economic benefit requires that above present refuse treatment rubbish is processed into a kind of calorific value, and composition is more even, and is stable, is easy to store; Proprietary pyrolysis reactor is a circulating fluidized bed, only uses self combustion gas as fluidized gas, does not have mechanical moving parts, utilizes fluidized gas to realize particle rubbish and high temperature circulation thermal barrier short mix, is rapidly heated and pyrolysis; One proprietary burner is set behind pyrolysis reactor, through pressure reduction the semicoke and the thermal barrier of pyrolysis reactor bottom is sent in the burner, the burning through semicoke comes the heat hot carrier, and does not need other auxiliary fuel; High-temperature flue gas in the burner sent in the garbage raw material moisture eliminator heat, garbage drying reduces water cut, has improved system thermal efficiency.
The beneficial effect of the utility model is embodied in:
The fine solution daily-life garbage without environmental pollution of domestic waste pyrolysis fuel oil equipment decapacitation, minimizing, and aspect energy utilization, have more significant advantage:
1, from rubbish, can directly obtain to be convenient to the oil fuel storing and carry at a distance.This liquid oil can also big standard be used in industry except that can generating electricity.Simultaneously the further processing of this liquid oil can be obtained the Chemicals of high added value;
2, applied widely, contain abundant organism in the most city domestic refuse, can pyrolysis;
3, significantly reduce the quality and the volume of domestic refuse through waste preprocessing technology;
4, from the material handling proximate analysis, the pyrolysis processing turndown ratio is big, and is strong to the flexibility of rubbish composition fluctuation;
5, the Dust Capacity of domestic garbage pyrolysis processing generation flue gas is few, the sulphur in the rubbish, and chlorine, oxious component major parts such as heavy metal are fixed in the final lime-ash, do not have secondary pollution basically;
6, pyrolytic process is simple, is easy to operate and control, and investment and working cost are low.
Description of drawings
Fig. 1 is the utility model process flow sheet.
Embodiment
With reference to Fig. 1; Domestic waste pyrolysis fuel oil equipment; Comprise trash repository 1, scraper conveyor 4, broken bag trommel screen 5, first rotary conveyor 4, the first rubbish trommel screen 7, letter sorting crusher 6, second rotary conveyor 9, magnetic separator 10, the second rubbish trommel screen 11, the 3rd rotary conveyor 12, half wet crushing mill 13, the 4th rotary conveyor 14, drying machine 15, stirring mixer 18, the 5th rotary conveyor 19, single-lead-screw extruding briquetting machine 20 and pyrolytic reaction equipment; The outlet of said trash repository 1 is connected with the import of said scraper conveyor 4; The outlet of said scraper conveyor 4 is connected with the import of said broken bag trommel screen 5; The outlet of said broken bag trommel screen 5 is connected with the import of said first rotary conveyor 4; The outlet of said first rotary conveyor 4 is connected with the import of the said first rubbish trommel screen 7; The import of the said letter sorting crusher 6 of the outlet of the said first rubbish trommel screen 7 links to each other, and the outlet of said letter sorting crusher 6 links to each other with 9 imports of said second rotary conveyor, and the outlet of said second rotary conveyor 9 links to each other with the import of said magnetic separator 10; The outlet of said magnetic separator 10 links to each other with the import of the said second rubbish trommel screen 11; The outlet of the said second rubbish trommel screen 11 links to each other with the import of said the 3rd rotary conveyor 12, and the outlet of said the 3rd rotary conveyor 12 links to each other with the import of said half wet crushing mill 13, and the outlet of said half wet crushing mill 13 links to each other with the import of said the 4th rotary conveyor 14; The outlet of said the 4th rotary conveyor 14 links to each other with the import of said drying machine 15; The outlet of said drying machine 15 links to each other with the import of stirring mixer 18, and the outlet of said stirring mixer 18 links to each other with the import of said the 5th rotary conveyor 19, and the outlet of said the 5th rotary conveyor 19 links to each other with the import of said single-lead-screw extruding briquetting machine 20; The outlet of said single-lead-screw extruding briquetting machine 20 links to each other with the import of said pyrolytic reaction equipment, and the outlet of said pyrolytic reaction equipment links to each other with the import of said moisture eliminator 15.
Further; Described pyrolytic reaction equipment comprises burner 25, first cyclonic separator 27, pyrolysis reactor 24, second cyclonic separator 29 and condensing surface 31; The import of described pyrolysis reactor 24 links to each other with the outlet of described single-lead-screw extruding briquetting machine 20; The outlet of said pyrolysis reactor 24 links to each other with the import of said second cyclonic separator 29; The outlet of said second cyclonic separator 29 links to each other through the import of blower fan 30 with said condensing surface 31, and the outlet of said condensing surface 31 links to each other with said pyrolysis reactor 24 through blower fan 33, and the bottom of said pyrolysis reactor 24 links to each other with said burner 25; The top of said burner 25 links to each other with the import of said first cyclonic separator 27, and the outlet of said first cyclonic separator 27 links to each other through the import of blower fan 28 with said moisture eliminator 15.
Further; Between described single-lead-screw extruding briquetting machine 20 and described pyrolysis reactor 24, also be provided with lift 21, temporary storing bin 22 and screw feeder 23; The outlet of described single-lead-screw extruding briquetting machine 20 links to each other with the import of described lift 21; The outlet of described lift 21 links to each other with the import of described temporary storing bin 22, and the outlet of described temporary storing bin 22 links to each other with the import of described screw feeder 23, and the outlet of described screw feeder 23 links to each other with the import of described pyrolysis reactor 24.
Further, the bottom of said burner 25 is provided with blower fan 26.
Further; The lower end side of said pyrolysis reactor 24 also is provided with screw feeder 35 and feed bin 34; One end of said screw feeder 35 links to each other with said pyrolysis reactor 24; The other end is connected with said feed bin 34, and the thermal barrier in the said feed bin 34 gets into through said screw feeder 35 and replenishes the thermal barrier that wears away in the said pyrolysis reactor 24.
Further, between said moisture eliminator 15 and said stirring mixer 18, be provided with electronic belt scale 16.
Further, the bottom of said condensing surface 31 is provided with basin 32.
Further, described half wet crushing mill 13 comprises pulverizing topworks, casing, frame and drive unit; Described drying machine 15 is the direct heating cocurrent drier, is provided with flight in the machine and conducts heat to guarantee the direct uniform contact of granulated garbage and flue gas; Said single-lead-screw extruding briquetting machine 20 is the built-up type Squeezinggranulator, by homogeneous, stirs, and combinations such as extrusion molding, the homogeneous mixing part is made up of twin shaft blade and casing, and the extrusion molding part is made up of reducing Variable pitch screw, discharging orifice plate and housing.
Two common difficulties that the utility model is run into the development of various countries, the world today---rubbish surplus and energy deficiency are organically coordinated.Its technological core is an integrated technique: the first step is with the domestic refuse pre-treatment, processes calorific value at 15-20MJ/Nm
3, water cut＜10%, the ingredient stability garbage raw material particle of ash content＜8%; Second step was that this granulated garbage is processed calorific value through fast pyrogenation is 15-18MJ/Nm
3Biofuel oil.This oil can directly use in industry, substitutes many boilers, mover and the used fuel oil of turbine; But also can therefrom extract a series of chemical substances, like foodstuff additive, resin, medicament etc.Because what generate is liquid fuel, so can store at an easy rate and transport, not limited by the region.
When the utility model uses, utilize driving grab bucket 2 from trash repository 1, to take out raw material rubbish, deliver in the receiving hopper 3 of refuse treatment production line, and deliver to brokenly rubbish in bag trommel screen 5 equably through scraper conveyor 4.Deliver to rubbish from cooking in the first rubbish trommel screen 7 with first rotary conveyor 8 as screen underflow less than the organism and the inorganics dirt of sieve aperture; Broken delivering to greater than the screen overflow of sieve aperture in the letter sorting crusher 6.Rubbish after fragmentation is sent in the magnetic separator 10 with second rotary conveyor 9 and further metal object is sorted out; Further screen underflow is got in the second rubbish trommel screen 11 then and sort.Less than the inorganics dirt of sieve aperture as the building materials raw material; Screen overflow rubbish is sent into the 3rd rotary conveyor 12 and is carried out the secondary pulverizing in rubbish half wet crushing mill 13.The advantage that secondary is pulverized is can moisture about 40% rubbish be pulverized, and extracts the rubbish of granularity＜20mm after the pulverizing.Rubbish after secondary is pulverized gets in the rotary shelf drier 15 through the 4th rotary conveyor 14 and carries out drying.After belted electronic balance 16 meterings, send in the continuously stirring mixing machine 18 through dried garbage raw material (moisture＜12%), simultaneously, additives such as CaO also mix in the adding stirring mixer 18 after belted electronic balance 16 meterings from feed bin 17 together again.Garbage raw material behind the uniform mixing is sent into by the 5th rotary conveyor 19 and is carried out homogeneous in the single-lead-screw extruding briquetting machine 20, stirs extrusion molding.Send into the temporary storing bin 22 with chapelet 21 from the garbage raw material particle (diameter＜Φ 15mm) that single-lead-screw extruding briquetting machine 20 comes out, evenly send in the pyrolysis reactor 24 through screw feeder 23 again.24 garbage gas that come from condensing surface 31 of pyrolysis reactor are as fluidizing medium.Get into pyrolysis reactor 24 interior granulated garbages and mix, and under fluidised situation, conduct heat with the thermal barrier that comes from burner 25, mass transfer, and be heated rapidly to 800 ℃, and pyrolysis rapidly; Oil gas after pyrolysis gets into second cyclonic separator 29 from the top exit of pyrolysis reactor 24 and isolates the ash content in the oil gas; The oil gas of sloughing ash content is sent in the condensing surface 31 cooling fast through blower fan 30 and is obtained liquid fuel oil and put into basin 32 and store.And the combustion gas that few part is not liquefied is sent in the pyrolysis reactor as fluidization gas through blower fan.The semicoke and the thermal barrier that come out from the pyrolysis reactor bottom get into the burner 25.Semicoke burns in burner 25 provides thermal source, and the temperature of thermal barrier is heated to about 1000 ℃.Flue gas and thermal barrier are discharged through the top of burner 25 and are got in first cyclonic separator 27, thermal barrier with get into again in the pyrolysis reactor 24 after flue gas separates, and flue gas is admitted to drying machine 15 garbage dryings through blower fan 28.Wherein the thermal barrier in the feed bin 34 gets into through screw feeder 35 and replenishes the thermal barrier that wears away in the pyrolysis reactor 24.
The described content of this specification sheets embodiment only is enumerating the way of realization of inventive concept; Should not being regarded as of the protection domain of the utility model only limits to the specific form that embodiment states, the protection domain of the utility model also reach in those skilled in the art conceive according to the present invention the equivalent technologies means that can expect.
Claims (7)
1. domestic waste pyrolysis fuel oil equipment; It is characterized in that: comprise trash repository, scraper conveyor, broken bag trommel screen, first rotary conveyor, the first rubbish trommel screen, letter sorting crusher, second rotary conveyor, magnetic separator, the second rubbish trommel screen, the 3rd rotary conveyor, half wet crushing mill, the 4th rotary conveyor, drying machine, stirring mixer, the 5th rotary conveyor, single-lead-screw extruding briquetting machine and pyrolytic reaction equipment; The outlet of said trash repository is connected with the import of said scraper conveyor; The outlet of said scraper conveyor is connected with the import of said broken bag trommel screen; The outlet of said broken bag trommel screen is connected with the import of said first rotary conveyor; The outlet of said first rotary conveyor is connected with the import of the said first rubbish trommel screen; The import of the said letter sorting crusher of the outlet of the said first rubbish trommel screen links to each other, and the outlet of said letter sorting crusher links to each other with the said second rotary conveyor import, and the outlet of said second rotary conveyor links to each other with the import of said magnetic separator; The outlet of said magnetic separator links to each other with the import of the said second rubbish trommel screen; The outlet of the said second rubbish trommel screen links to each other with the import of said the 3rd rotary conveyor, and the outlet of said the 3rd rotary conveyor links to each other with the import of said half wet crushing mill, and the outlet of said half wet crushing mill links to each other with the import of said the 4th rotary conveyor; The outlet of said the 4th rotary conveyor links to each other with the import of said drying machine; The outlet of said drying machine links to each other with the import of stirring mixer, and the outlet of said stirring mixer links to each other with the import of said the 5th rotary conveyor, and the outlet of said the 5th rotary conveyor links to each other with the import of said single-lead-screw extruding briquetting machine; The outlet of said single-lead-screw extruding briquetting machine links to each other with the import of said pyrolytic reaction equipment, and the outlet of said pyrolytic reaction equipment links to each other with the import of said moisture eliminator.
2. domestic waste pyrolysis fuel oil equipment as claimed in claim 1; It is characterized in that: described pyrolytic reaction equipment comprises burner, first cyclonic separator, pyrolysis reactor, second cyclonic separator and condensing surface; The import of described pyrolysis reactor links to each other with the outlet of described single-lead-screw extruding briquetting machine; The outlet of said pyrolysis reactor links to each other with the import of said second cyclonic separator; The outlet of said second cyclonic separator links to each other with the import of said condensing surface through blower fan, and the outlet of said condensing surface links to each other with said pyrolysis reactor through blower fan, and the bottom of said pyrolysis reactor links to each other with said burner; The top of said burner links to each other with the import of said first cyclonic separator, and the outlet of said first cyclonic separator links to each other with the import of said moisture eliminator through blower fan.
3. domestic waste pyrolysis fuel oil equipment as claimed in claim 2; It is characterized in that: between described single-lead-screw extruding briquetting machine and described pyrolysis reactor, also be provided with lift, temporary storing bin and screw feeder; The outlet of described single-lead-screw extruding briquetting machine links to each other with the import of described lift; The outlet of described lift links to each other with the import of described temporary storing bin; The outlet of described temporary storing bin links to each other with the import of described screw feeder, and the outlet of described screw feeder links to each other with the import of described pyrolysis reactor.
4. domestic waste pyrolysis fuel oil equipment as claimed in claim 3, it is characterized in that: the bottom of said burner is provided with blower fan.
5. domestic waste pyrolysis fuel oil equipment as claimed in claim 4; It is characterized in that: the lower end side of said pyrolysis reactor also is provided with screw feeder and feed bin; One end of said screw feeder links to each other with said pyrolysis reactor; The other end is connected with said feed bin, and the thermal barrier in the said feed bin gets into through said screw feeder and replenishes the thermal barrier that wears away in the said pyrolysis reactor.
6. domestic waste pyrolysis fuel oil equipment as claimed in claim 5 is characterized in that: between said moisture eliminator and said stirring mixer, be provided with electronic belt scale.
7. domestic waste pyrolysis fuel oil equipment as claimed in claim 6, it is characterized in that: the bottom of said condensing surface is provided with basin.
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| CN2012201708729U CN202543162U (en) | 2012-04-20 | 2012-04-20 | Device for pyrolyzing urban garbage for generating fuel oil |
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| CN2012201708729U CN202543162U (en) | 2012-04-20 | 2012-04-20 | Device for pyrolyzing urban garbage for generating fuel oil |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105921498A (en) * | 2016-06-17 | 2016-09-07 | 北京神雾环境能源科技集团股份有限公司 | Household garbage resourceful comprehensive treatment method and treatment system |
| CN105921497A (en) * | 2016-06-17 | 2016-09-07 | 北京神雾环境能源科技集团股份有限公司 | Resourceful comprehensive treatment method and system for household garbage |
| CN106077029A (en) * | 2016-06-17 | 2016-11-09 | 北京神雾环境能源科技集团股份有限公司 | Domestic garbage resource integrated conduct method and processing system |
| CN106111675A (en) * | 2016-08-12 | 2016-11-16 | 北京神雾环境能源科技集团股份有限公司 | Domestic garbage resource integrated conduct method and processing system |
| CN106111657A (en) * | 2016-06-17 | 2016-11-16 | 北京神雾环境能源科技集团股份有限公司 | Domestic garbage resource integrated conduct method and processing system |
| CN106391671A (en) * | 2016-11-28 | 2017-02-15 | 北京华福工程有限公司 | Household garbage pretreatment method suitable for garbage pyrolysis and pretreatment object |
| CN111644450A (en) * | 2020-06-29 | 2020-09-11 | 盐城工学院 | Organic household garbage treatment system and method |
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2012
- 2012-04-20 CN CN2012201708729U patent/CN202543162U/en not_active Expired - Lifetime
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105921498A (en) * | 2016-06-17 | 2016-09-07 | 北京神雾环境能源科技集团股份有限公司 | Household garbage resourceful comprehensive treatment method and treatment system |
| CN105921497A (en) * | 2016-06-17 | 2016-09-07 | 北京神雾环境能源科技集团股份有限公司 | Resourceful comprehensive treatment method and system for household garbage |
| CN106077029A (en) * | 2016-06-17 | 2016-11-09 | 北京神雾环境能源科技集团股份有限公司 | Domestic garbage resource integrated conduct method and processing system |
| CN106111657A (en) * | 2016-06-17 | 2016-11-16 | 北京神雾环境能源科技集团股份有限公司 | Domestic garbage resource integrated conduct method and processing system |
| CN106111675A (en) * | 2016-08-12 | 2016-11-16 | 北京神雾环境能源科技集团股份有限公司 | Domestic garbage resource integrated conduct method and processing system |
| CN106391671A (en) * | 2016-11-28 | 2017-02-15 | 北京华福工程有限公司 | Household garbage pretreatment method suitable for garbage pyrolysis and pretreatment object |
| CN111644450A (en) * | 2020-06-29 | 2020-09-11 | 盐城工学院 | Organic household garbage treatment system and method |
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