CN103982897A - Incinerator system - Google Patents
Incinerator system Download PDFInfo
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- CN103982897A CN103982897A CN201410230763.5A CN201410230763A CN103982897A CN 103982897 A CN103982897 A CN 103982897A CN 201410230763 A CN201410230763 A CN 201410230763A CN 103982897 A CN103982897 A CN 103982897A
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- incinerator
- incineration
- air
- incinerator system
- stove
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Abstract
The invention relates to an incinerator system. The incinerator system comprises a feeding port, an incinerator, a spiral belt feeder, a cyclone separator, an air exhaust fan, a direct fire furnace, a heat exchanger, a spiral conveyer and an oil tank. According to the incinerator system, a furnace body of the incinerator system is sealed, the interior of the incinerator works under negative pressure, smoke can be effectively prevented, a novel smash shaft is arranged in the incinerator, incineration materials can be conveyed and discharged while the novel smash shaft is smashing the incineration materials, the superficial area of the incineration materials after being smashed can be increased, incineration is even and full, and incineration efficiency is high. The incinerator system incinerates the incineration materials by using high temperature hot wind which is blown in, can reduce discharge amount of tail gas, can adjust incineration temperature to be appropriate according to different incineration materials so as to avoid unnecessary loss of beneficial ingredients in the incineration materials and guarantee recycling utilization of additional value of secondary materials, can save energy and protect environment well due to the fact no unnecessary heat is input, and cleanly discharges tail gas due to the fact that waste heat in each link can be recycled.
Description
Technical field
The present invention relates to incinerator field, relate in particular to a kind of Novel incineration furnace.
Background technology
There is variety of issue in domestic existing incinerator system, such as incinerated matter in stove easily lumps, has influence on the burning effect of incinerator, causes burning insufficient.And cylinder sealing adopts the directly mode of laminating, cause sealing property decline after long term wear, heat energy loss is serious, pollutes surrounding enviroment.And the outer indirect of stove or naked light directly burn, easily cause incinerated matter to lump after burning, the unnecessary beneficiating ingredient loss only of burn.Waste heat recovery is abundant not, thereby production efficiency is low.
In addition, also existing incineration temperature to fix can not regulate according to different incinerated matters, and secondary thing is difficult to recycling.
In order to solve the variety of issue existing in above-mentioned prior art, the application provides a kind of novel CIU, and it can reach following technique effect.
For incinerated matter, in salamander phenomenon, Novel incineration furnace system has adopted the middle broken shaft High Rotation Speed of special spiral structure, thereby avoids salamander, incinerated matter is had to broken and conveying effect simultaneously.And settle baffle plate at inner wall of rotary drum, and be screw arrangement, incinerated matter is carried forward in stirring.After fragmentation, greatly increased the surface area of incinerated matter, more evenly, fully, efficiency is higher in burning.
More rational spring pressuring plate hermetically-sealed construction is taked in the cylinder sealing of incinerator, after meeting long-term running, can fit well all the time, ensure high leakproofness, in stove, adopt micro-vacuum state, there is part leakage point even if textural, furnace gas after burning and dust can not leak to outside yet, and can effectively prevent flue gas, and dust leaks in body of heater.
And the burning mode of this CIU adopts high-temperature hot-air, directly contacted with incinerated matter by high-temperature hot-air, this kind of mode is the very high one of efficiency in incinerator.
Aspect waste heat recovery, novel CIU has taken into full account the recycling residual heat of links, comprising the easiest uncared-for waste heat in top; Purification has also been considered in the discharge of tail gas.
The temperature of whole CIU is adjustable controlled, control by the quantity to burner, can be adjusted to suitable incineration temperature according to different incinerated matters at any time, avoid the unnecessary loss of beneficiating ingredient in incinerated matter, the added value that ensures secondary thing is recycled, and do not make unnecessary heat and drop into, can be energy-conservation better.
Summary of the invention
The object of the present invention is to provide a kind of Novel incineration furnace system, it can increase the surface area of incinerated matter, burn more evenly, fully, efficiency is higher, can regulate suitable incineration temperature according to different incinerated matters, avoid the unnecessary loss of beneficiating ingredient in incinerated matter, the added value that ensures secondary thing is recycled, and does not make unnecessary heat and drop into, energy-conserving and environment-protective better, and the waste heat energy of links recycles, the discharge of tail gas is cleaner.
Technical scheme of the present invention is: a kind of incinerator system, comprise charging aperture, incinerator, ribbon feeder, cyclone separator, air exhauster, straight stove, heat exchanger, conveying worm and oil tank, feed pipe one end on wherein said incinerator is connected with ribbon feeder, the setting of described ribbon feeder is connected to charging aperture, the other end of described incinerator is connected to cyclone separator, described cyclone separator is further connected to described exhaust fan by pipeline, described exhaust fan connects described heat exchanger, and described incinerator is also connected to straight stove by high-temperature hot-air air channel, described straight stove is connected to described heat exchanger by waste-heat air channel, described heat exchanger is connected to tail gas tabacco barn by flue, incinerated matter is discharged by described conveying worm, described oil tank is connected to described straight stove by pipeline.
Further, in described ribbon feeder, spiral helicine ribbon is installed, and in described incinerator, broken shaft is installed, on described broken shaft, helically is provided with broken blade.
Further, described incinerator has cylinder, and spring pressuring plate structure is arranged in described cylinder sealing.
Further, described charging aperture adopts closed structure, and while feeding intake, effectively the cold air of blocking-up dog-house enters in the cylinder of described incinerator.
Further, the oil plant in described oil tank is transported in described straight stove and is burnt by pipeline, and the high-temperature hot-air institute after burning is by sending into described incinerator in described high-temperature hot-air air channel, and high-temperature hot-air directly contacts with incinerated matter.
Further, described cylinder inside is provided with baffle plate, and described baffle plate is helical type and distributes.
Further, in described straight stove, be provided with multiple burners, it can control combustion oil mass.
In sum, the invention has the beneficial effects as follows: (1) this Novel incineration furnace system has adopted the middle broken shaft High Rotation Speed of special spiral structure, thereby avoid salamander, incinerated matter is had to the surface area that has greatly increased incinerated matter after broken and conveying effect fragmentation simultaneously, burn more evenly, fully, efficiency is higher; (2) more rational spring pressuring plate structure is taked in cylinder sealing, can ensure high leakproofness, adopts micro-vacuum state in stove, effectively prevents flue gas, and the furnace gas after burning and dust can not leak to outside yet; (3) burning mode adopts high-temperature hot-air, is directly contacted with incinerated matter by high-temperature hot-air, and firing efficiency is very high, simultaneously the service life of energy extension device; (4) this novel CIU has taken into full account that the waste heat recovery of links recycles; (5) temperature of this novel whole CIU is adjustable controlled, can be adjusted to suitable incineration temperature according to different incinerated matters, avoid the unnecessary loss of beneficiating ingredient in incinerated matter, the added value that ensures secondary thing is recycled, and do not make unnecessary heat and drop into, energy-conserving and environment-protective better.
Be described in more detail the present invention below by specific embodiment.
Brief description of the drawings
Fig. 1 is the structural representation of incinerator system of the present invention;
Fig. 2 is the structural representation of the incinerator in incinerator system of the present invention;
Fig. 3 is the structural representation of the broken shaft in incinerator.
Fig. 4 is the operation logic schematic diagram of incinerator system of the present invention.
Detailed description of the invention
Below in conjunction with accompanying drawing, 1-4 is further described the present invention with embodiment.But protection scope of the present invention is not limited to this.
As shown in Figure 1, it shows the concrete structure of incinerator system of the present invention, this incinerator system comprises charging aperture 1, incinerator 3, ribbon feeder 2, cyclone separator 4, air exhauster 5, straight stove 9, heat exchanger 7, conveying worm 12 and oil tank 13, wherein the feed pipe one end on incinerator 3 is connected with ribbon feeder 2, ribbon feeder 2 arranges and is connected to charging aperture 1, the incinerated matter burning when needs is sent to after charging aperture 1, ribbon feeder 2 can be sent to incinerator 3 by incinerated matter by inner helical form ribbon, charging aperture 1 adopts closed structure, the cold air that can effectively block dog-house when incinerated matter is fed intake further enters in the burning cylinder of incinerator 3, improve the thermal efficiency.The broken shaft of dog-house effectively prevents the obstruction of material, and after coarse crushing, increase the surface area of material, thereby more fully promptly carry out heat conduction, improve the evaporation rate of moisture, and the spirality ribbon of ribbon feeder 2 can quantitatively feed intake, and makes necessarily to burn output, normal burning is played the circulation of air between blocking-up dog-house 1 and the burning cylinder of incinerator in producing simultaneously, opened circuit in air channel, be unlikely to make incinerator to produce thermal loss.The other end of described incinerator 3 is connected to cyclone separator 4, cyclone separator 4 separates the emission having burned with flue gas, and cyclone separator 4 is further connected to described air exhauster 5 by pipeline, by air exhauster 5, flue gas is discharged, described exhaust fan 5 further arrives and connects heat exchanger 7, heat exchanger 7 gets up the residual heat collection in flue gas, and as shown in Figure 1, incinerator 3 is also connected to straight stove 9 by high-temperature hot-air air channel 10, in straight stove 9, there are multiple burners, its quantity can increase or reduce, also can control combustion oil mass, thereby can regulate the problem of high-temperature hot-air, further regulate the incineration temperature of incinerator, rubbish burning can not lumpd, and the waste heat that straight stove 9 fuel combustions produce can be connected to described heat exchanger 7 by waste-heat air channel 8, heat exchanger 7 is recycled waste heat, heat exchanger 7 is connected to tail gas funnel 6 by flue, tail gas after heat recovery can be discharged by tail gas funnel 6, heat after heat exchanger 7 reclaims is supplied with to straight stove and is utilized, the incinerated matter 11 of simultaneously separating in cyclone separator 4 is discharged by described conveying worm 12, described oil tank 13 is connected to described straight stove 9 by pipeline, straight stove 9 is carried out to fuel supply.
As shown in Figure 2, it is the structural representation of incinerator in native system, wherein clearly can find out, spirality ribbon is installed in ribbon feeder 2, and broken shaft 15 is installed in incinerator 3, as shown in Figure 3, on broken shaft 15, helically is provided with broken blade, when system running, broken shaft 15 in incinerator can, according to the rotation of charging degree, make the refinement of piece thing, further increases the surface area of incinerated matter, effectively prevent the accumulation of incinerated matter in stove, also handlebar burns and expects to carry to the cyclone separator 4 of outlet simultaneously.As seen from Figure 2, incinerator 3 has cylinder, and the structure of spring pressuring plate 14 is arranged in cylinder sealing, and spring pressuring plate is gluing, sealing all the time, and cylinder inside is provided with baffle plate, and described baffle plate is helical type and distributes, and special baffle plate can stirring no backup.Because body of heater adopts hermetically-sealed construction, furnace pressure is micro-negative pressure, avoids furnace gas to leak.Be provided with cleaning door 16 in the bottom of incinerator 3.
Fig. 4 is the operational flow diagram of CIU of the present invention, as shown in Figure 4, the rubbish reclaiming is put into ribbon feeder 2 by charging aperture 1, ribbon feeder 2 is quantitatively put into rubbish incinerator 3, broken shaft in incinerator 3 runs up refuse breaking, meanwhile, oil plant in oil tank 13 is transported to burning in straight stove 9 by pipeline, high-temperature hot-air institute after burning is by sending into described incinerator in described high-temperature hot-air air channel 10, high-temperature hot-air directly contacts with broken incinerated matter in the cylinder of incinerator, incinerated matter is fully burned, waste material after burning is transported to cyclone separator 4 with flue gas and separates, rotation baiting valve after separating in cyclone separator 4 is opened, by incinerated matter 11 cooling and discharge by conveying worm, burn the flue gas producing simultaneously and be discharged to heat exchanger 7 by air exhauster 5, by waste heat recovery, flue gas after waste heat recovery passes through tail gas funnel 6 after purified treatment, the institute that heat exchanger 7 reclaims simultaneously has surplus heat to supply with and recycles to straight stove 9.
As previously mentioned, dog-house of the present invention adopts closed structure, and while feeding intake, effectively the cold air of blocking-up dog-house enters and burns cylinder, improves the thermal efficiency.The broken shaft of dog-house effectively prevents the obstruction of material, and after coarse crushing, has increased the surface area of material, thereby more fully promptly carries out heat conduction, improves the evaporation rate of moisture.Ribbon feeder quantitatively feeds intake, and makes certain output, plays blocking-up input port simultaneously and burn the circulation of air between cylinder in normal production, is opened circuit in air channel.Broken shaft High Rotation Speed in stove, make the refinement of piece thing, further increase the surface area of incinerated matter, effectively prevent the accumulation of incinerated matter in stove simultaneously, also handlebar burns the effect that material is carried to outlet, in stove, adopt micro-vacuum state, occur part leakage point even if textural, the furnace gas after burning and dust can not leak to outside yet.The burning mode that adopts high-temperature hot-air to be blown into, can set different incineration temperatures according to different sorting rubbish, thereby reduces the discharge capacity of tail gas, retains the value composition of organic waste simultaneously, so that be worth the recycling of part.The design of stove Internal baffle is unique, makes burning away the refuse in stove in stove, stir and discharge outside stove, has avoided rubbish to be detained in stove.
Due to above structural design, this CIU production efficiency is high, can utilize waste heat, thereby energy consumption is lower, and native system can also be as drying machine use, uniform drying, and the service life of native system is longer in addition.
CIU of the present invention can be widely used in treatment of urban garbage, rubbish charing is the every field such as turning sludge into fuel, food debris processing, chemical plant activated sludge, excrement of animals, plant fibre slag processing, metal water acidification, can carry out to greatest extent using energy source and environmental protection.
Above-mentioned disclosed be only the preferred embodiment of CIU of the present invention, preferred embodiment does not have all details of detailed descriptionthe, does not limit invention only for described detailed description of the invention yet.Obviously according to the content of this description, can do a lot of modifications and variations, this description choose specifically describe these embodiment be for explain better of the present invention away from and practical application, thereby make one of ordinary skill in the art can utilize well the present invention, the present invention is only subject to the restriction of claim and four corner and equivalent.
Claims (7)
1. an incinerator system, comprise charging aperture, incinerator, ribbon feeder, cyclone separator, air exhauster, straight stove, heat exchanger, conveying worm and oil tank, feed pipe one end on wherein said incinerator is connected with ribbon feeder, the setting of described ribbon feeder is connected to charging aperture, the other end of described incinerator is connected to cyclone separator, described cyclone separator is further connected to described exhaust fan by pipeline, described exhaust fan connects described heat exchanger, and described incinerator is also connected to straight stove by high-temperature hot-air air channel, described straight stove is connected to described heat exchanger by waste-heat air channel, described heat exchanger is connected to tail gas tabacco barn by flue, incinerated matter is discharged by described conveying worm, described oil tank is connected to described straight stove by pipeline.
2. according to the incinerator system described in claim 1, it is characterized in that: in described ribbon feeder, spiral helicine ribbon is installed, and in described incinerator, broken shaft is installed, on described broken shaft, helically is provided with broken blade.
3. according to the incinerator system described in claim 1, it is characterized in that: described incinerator has cylinder, spring pressuring plate hermetically-sealed construction is arranged in described cylinder sealing.
4. according to the incinerator system described in claim 3, it is characterized in that: described charging aperture adopts closed structure, while feeding intake, effectively the cold air of blocking-up dog-house enters in the cylinder of described incinerator.
5. according to the incinerator system described in claim 1, it is characterized in that: the oil plant in described oil tank is transported in described straight stove and is burnt by pipeline, high-temperature hot-air institute after burning is by sending into described incinerator in described high-temperature hot-air air channel, and high-temperature hot-air directly contacts with incinerated matter.
According to described in claim 3 incinerator system, it is characterized in that: described cylinder inside is provided with baffle plate, described baffle plate be helical type distribute.
7. incinerator system according to claim 1, is characterized in that: in described straight stove, be provided with multiple burners, it can control combustion oil mass.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410230763.5A CN103982897B (en) | 2014-03-19 | 2014-05-29 | A kind of incinerator system |
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410101420.9 | 2014-03-19 | ||
| CN2014101014209 | 2014-03-19 | ||
| CN201410101420 | 2014-03-19 | ||
| CN201410230763.5A CN103982897B (en) | 2014-03-19 | 2014-05-29 | A kind of incinerator system |
Publications (2)
| Publication Number | Publication Date |
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| CN103982897A true CN103982897A (en) | 2014-08-13 |
| CN103982897B CN103982897B (en) | 2017-08-29 |
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| CN201410230763.5A Expired - Fee Related CN103982897B (en) | 2014-03-19 | 2014-05-29 | A kind of incinerator system |
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Citations (13)
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|---|---|---|---|---|
| EP0692679A2 (en) * | 1994-07-13 | 1996-01-17 | Klöckner-Humboldt-Deutz Aktiengesellschaft | Method and plant layout for drying and incinerating sewage sludge |
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| JP2001227729A (en) * | 2000-02-15 | 2001-08-24 | Susumu Nakada | Incinerator |
| CN2545485Y (en) * | 2002-04-16 | 2003-04-16 | 吴桐 | Medical refuse treating system |
| CN1523266A (en) * | 2003-02-20 | 2004-08-25 | 徐宝安 | Process and apparatus for erasing fly ash containing dioxin of refuse burning boiler by incineration |
| CN1987202A (en) * | 2005-12-21 | 2007-06-27 | 中国科学院大连化学物理研究所 | Method and its device for garbage burning and flyash incinerating treatment |
| CN101117261A (en) * | 2007-07-18 | 2008-02-06 | 浙江环兴机械有限公司 | Sludge drying burning treatment method and integrated apparatus |
| CN201145280Y (en) * | 2007-10-25 | 2008-11-05 | 中国石油天然气股份有限公司 | Oily scum incineration treatment device |
| CN201462857U (en) * | 2009-07-15 | 2010-05-12 | 史海峰 | Mould sludge incinerator |
| CN201476486U (en) * | 2009-07-29 | 2010-05-19 | 中橡集团炭黑工业研究设计院 | Sealing device of rotary dryer |
| CN201772465U (en) * | 2010-09-08 | 2011-03-23 | 安徽海螺川崎节能设备制造有限公司 | Refuse burning device |
| CN201795495U (en) * | 2010-07-21 | 2011-04-13 | 安徽海螺集团有限责任公司 | Refuse disposal system |
| CN102242003A (en) * | 2010-05-12 | 2011-11-16 | 武汉海德新能源投资有限公司 | Composite type oxygen-enriching biomass gasification furnace |
-
2014
- 2014-05-29 CN CN201410230763.5A patent/CN103982897B/en not_active Expired - Fee Related
Patent Citations (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0692679A2 (en) * | 1994-07-13 | 1996-01-17 | Klöckner-Humboldt-Deutz Aktiengesellschaft | Method and plant layout for drying and incinerating sewage sludge |
| CN2400694Y (en) * | 2000-01-05 | 2000-10-11 | 北京通用能源动力公司 | Fluidized-bed refuse incinerator |
| JP2001227729A (en) * | 2000-02-15 | 2001-08-24 | Susumu Nakada | Incinerator |
| CN2545485Y (en) * | 2002-04-16 | 2003-04-16 | 吴桐 | Medical refuse treating system |
| CN1523266A (en) * | 2003-02-20 | 2004-08-25 | 徐宝安 | Process and apparatus for erasing fly ash containing dioxin of refuse burning boiler by incineration |
| CN1987202A (en) * | 2005-12-21 | 2007-06-27 | 中国科学院大连化学物理研究所 | Method and its device for garbage burning and flyash incinerating treatment |
| CN101117261A (en) * | 2007-07-18 | 2008-02-06 | 浙江环兴机械有限公司 | Sludge drying burning treatment method and integrated apparatus |
| CN201145280Y (en) * | 2007-10-25 | 2008-11-05 | 中国石油天然气股份有限公司 | Oily scum incineration treatment device |
| CN201462857U (en) * | 2009-07-15 | 2010-05-12 | 史海峰 | Mould sludge incinerator |
| CN201476486U (en) * | 2009-07-29 | 2010-05-19 | 中橡集团炭黑工业研究设计院 | Sealing device of rotary dryer |
| CN102242003A (en) * | 2010-05-12 | 2011-11-16 | 武汉海德新能源投资有限公司 | Composite type oxygen-enriching biomass gasification furnace |
| CN201795495U (en) * | 2010-07-21 | 2011-04-13 | 安徽海螺集团有限责任公司 | Refuse disposal system |
| CN201772465U (en) * | 2010-09-08 | 2011-03-23 | 安徽海螺川崎节能设备制造有限公司 | Refuse burning device |
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| CN103982897B (en) | 2017-08-29 |
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