CN205316331U - High -efficient short schizolysis second combustion chamber rubbish thermal cracking heat energy reborner - Google Patents
High -efficient short schizolysis second combustion chamber rubbish thermal cracking heat energy reborner Download PDFInfo
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- CN205316331U CN205316331U CN201521064380.1U CN201521064380U CN205316331U CN 205316331 U CN205316331 U CN 205316331U CN 201521064380 U CN201521064380 U CN 201521064380U CN 205316331 U CN205316331 U CN 205316331U
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- heater
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- dual firing
- thermal cracking
- pipe
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- 239000010813 municipal solid waste Substances 0.000 title claims abstract description 40
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 26
- 238000004227 thermal cracking Methods 0.000 title claims abstract description 24
- 238000010304 firing Methods 0.000 claims abstract description 42
- 238000009833 condensation Methods 0.000 claims abstract description 36
- 230000005494 condensation Effects 0.000 claims abstract description 36
- 239000002918 waste heat Substances 0.000 claims abstract description 28
- 239000007789 gas Substances 0.000 claims abstract description 21
- 239000011229 interlayer Substances 0.000 claims abstract description 7
- 239000003517 fume Substances 0.000 claims abstract description 5
- 239000010410 layer Substances 0.000 claims abstract description 5
- 230000009977 dual effect Effects 0.000 claims description 41
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 28
- 238000005336 cracking Methods 0.000 claims description 18
- 238000011084 recovery Methods 0.000 claims description 14
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 8
- 239000003546 flue gas Substances 0.000 claims description 8
- 239000000779 smoke Substances 0.000 claims description 8
- 238000009413 insulation Methods 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 4
- 238000012546 transfer Methods 0.000 claims description 4
- 230000015572 biosynthetic process Effects 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims description 3
- 238000007598 dipping method Methods 0.000 claims description 3
- 206010022000 influenza Diseases 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 6
- 239000001301 oxygen Substances 0.000 abstract description 6
- 229910052760 oxygen Inorganic materials 0.000 abstract description 6
- 239000007788 liquid Substances 0.000 abstract description 3
- 238000000926 separation method Methods 0.000 abstract description 3
- 238000010248 power generation Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 8
- 238000000197 pyrolysis Methods 0.000 description 5
- 238000009423 ventilation Methods 0.000 description 4
- 239000002689 soil Substances 0.000 description 3
- 150000001335 aliphatic alkanes Chemical class 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000002737 fuel gas Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 description 1
- 235000002918 Fraxinus excelsior Nutrition 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 239000002956 ash Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 229910000037 hydrogen sulfide Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000012188 paraffin wax Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
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- Incineration Of Waste (AREA)
Abstract
The utility model discloses a high -efficient short schizolysis second combustion chamber rubbish thermal cracking heat energy reborner, it includes the furnace body, and its inside is provided with the owner and fires the room, and the top is provided with dog -house and bell board, the furnace body inner chamber all around be the hollow interlayer structure, and the intermediate layer cut off mutually about being divided into two -layer, the top sets up to being used for vapor refrigerated condensation chamber in the stove, the below is for firing the second combustion chamber that the room feeds through with main, the gas -liquid separation system of intercommunication condensation chamber bottom is provided with in the outside in condensation chamber, the bottom of furnace body is provided with waste heat power generation system, furnace body side and bottom are connected with the blower system, and the right side of furnace body is provided with the fume emission mouth. The utility model provides a high -efficient short schizolysis second combustion chamber rubbish thermal cracking heat energy reborner optimizes blast air oxygen supply pipe way, promotes that rubbish fully burns, reduces the exhaust emissions to make full use of thermal cracking furnace's waste heat increases thermal cracking furnace's hot combustion efficiency.
Description
Technical field
The invention belongs to field of garbage disposal, be specially a kind of efficiently short cracking dual firing chamber rubbish thermal cracking heat energy reburner.
Background technology
Along with the quickening of economic development and urbanization, the quantity that annual domestic waste produces is multiplied. The traditional approach of garbage disposal is to build refuse landfill, is filled by rubbish. There is many drawbacks in this mode, first takies a large amount of soil exactly to build landfill yard, and soil is non-renewable resource, and land resource is pretty nervous; Second, after the material such as large amount of organic and battery enters landfill yard, the poisonous percolate of its generation will bring severe contamination to soil and groundwater, consider from the angle of environmental protection, have to set up that percolate from garbage filling field is impermeable, collection processing system implementing, this difficulty that will develop skill, also increases investment simultaneously, fills complicated operation, manage also highly difficult, additionally, the waste gas such as the methane of landfill yard, hydrogen sulfide also must be handled well, to guarantee explosion-proof and environmental requirement; Its three, a large amount of dumpings are in landfill yard, and the matter and energy wherein contained cannot be obtained by, and according to the viewpoint of recycling economy, this is also a kind of wasting of resources. Because landfill has such drawback, seldom adopt in this simple process mode of developed country at present.
, when thermal cracking rubbish, burning insufficient in existing combustion furnace, it is easy to produces bigger smoke pollution, bring difficulty to subsequent treatment; And the thermal conversion efficiency of pyrocrack furnace is low, waste heat waste is many, causes bigger pollution and waste. There is the space of bigger improvement in existing crucible garbage cracking.
Summary of the invention
It is an object of the invention to for problem above, it is provided that a kind of efficiently short cracking dual firing chamber rubbish thermal cracking heat energy reburner, optimize air blast ventilation channel, promote that rubbish fully burns, minimizing exhaust emissions, and make full use of the waste heat of pyrocrack furnace, the hot efficiency of combustion of gain of heat pyrolysis furnace.
For realizing object above, the technical solution used in the present invention is: a kind of efficiently short cracking dual firing chamber rubbish thermal cracking heat energy reburner, it includes body of heater (1), and it is internally provided with main combustion chamber (101), is provided above dog-house and stove cover plate;Described body of heater inner chamber surrounding is hollow interlayer structure, and interlayer is divided into two-layer blocked up and down, being provided above as the condensation chamber (2) of steam cooling in stove, lower section is the dual firing chamber (3) connected with main combustion chamber (101); Arranged outside at condensation chamber (2) has the Separate System of Water-jet (6) of connection condensation chamber (2) bottom; The bottom of described body of heater (1) is provided with afterheat generating system (4), described body of heater (1) side and bottom are connected to blower system (5), and the right side of body of heater (1) is provided with fume emission mouth (104);
Described afterheat generating system (4) includes the first waste heat recovery oil tank (401) being arranged on the bottom of body of heater (1) and the second waste heat recovery oil tank (402) being arranged on body of heater (1) sidepiece; And first waste heat recovery oil tank (401) and the second waste heat recovery oil tank (402) be connected to TRT by oil pipe (403).
Further, described condensation chamber (2) includes and the side plate (201) of body of heater (1) inwall formation air inlet, condensation chamber (2) is internal is provided with some S shape flues by flue gas dividing plate (202), and condensation chamber (2) lower section is connected with the Separate System of Water-jet (6) of outside distribution.
Further, flue gas dividing plate (202) horizontally set of described condensation chamber (2), and the both sides of condensation chamber (2) are provided with heat-insulation chamber (203), condensation chamber (2) be arranged below outward-dipping swash plate (204).
Further, described Separate System of Water-jet (6) includes the overflow pipe (601) being connected to condensation chamber (2) bottom, each overflow pipe (601) is communicated on upper strata conveying pipe (603) of body of heater (1) arranged outside, and upper strata conveying pipe (603) passes on left trap (607) and is connected to drain pipe (9); Right side, upper strata conveying pipe (603) connects the upper end of gas and water separator (604), gas and water separator (604) bottom is connected to drain pipe (609), and the upper end opposite side of gas and water separator (604) connects second blower fan (511) of blower system (5) by smoke extracting tube (606).
Further, the trap (607) in left side, described upper strata conveying pipe (603) is connected to drain pipe (9) by vertically height lower than the draining intervalve (608) on upper strata conveying pipe (603), and the vertically height of drain pipe (9) is lower than the height of draining intervalve (608); The transfer tube (605) of elbow-shaped it is connected between upper end and the smoke extracting tube (606) of described gas and water separator (604).
Further, described overflow pipe (601) end faces outwards is provided with upper strata observation panel (602), and overflow pipe (601) is connected with upper strata conveying pipe (603) by the connecting tube being arranged below.
Further, described blower system (5) includes the first blower fan (501), the first air main (502) being connected with the first blower fan (501), and the first air main (502) is linked into the side bottom of body of heater (1) by the sidewall air supply pipe (503) that body of heater (1) both sides are arranged; Several spaced bottom ajutages (514) that the air inlet of the second blower fan (511) is arranged below with body of heater (1) are connected.
Further, described dual firing chamber (3) is connected with main combustion chamber (101) by the hole of polylith swash plate (301) interval composition near the side of body of heater (1) inner chamber; And sidewall air supply pipe (503) is connected to the air vent (302) that dual firing chamber (3) bottom is arranged.
Further, described second blower fan (511) is communicated to bottom ajutage (514) by the second air main (512) and the air-supply intervalve (513) that is connected with the second air main (512); Described bottom ajutage (514) is communicated to body of heater (1) interior bottom, and is covered with above it for ventilated arc mesh blast cap (102).
Further, described dual firing chamber (3) is internally provided with residual neat recovering system (7), described residual neat recovering system (7) includes being arranged in the waste heat water pipe (701) that the internal S shape of dual firing chamber (3) is arranged, and the fixing seat (703) of water pipe being used for fixing waste heat water pipe (701), and supplied water with outer loop by the waterpipe jointing (702) arranged in the left hand external of body of heater (1).
Beneficial effects of the present invention: a kind of efficiently short cracking dual firing chamber of present invention rubbish thermal cracking heat energy reburner, optimize air blast ventilation channel, promote that rubbish fully burns, reduce exhaust emissions, and make full use of the waste heat of pyrocrack furnace, the hot efficiency of combustion of gain of heat pyrolysis furnace.
1, present invention employs the structure of condensation chamber, conveniently the steam in rubbish is liquefied rapidly, and intercept major part flue gas, facilitate the later stage to carry out gas-liquid separation.
2, the present invention adopts Separate System of Water-jet, conveniently realizes gas-liquid separation; Tail gas is passed in pyrocrack furnace simultaneously and burn, it is to avoid high alkane value gas enters vent gas treatment program, reduce the burden of later stage process.
3, the present invention has been specifically designed the dual firing chamber's structure except main combustion chamber, the paraffin gas that rubbish in the main combustion chamber being produces under thermal cracking fully burns in dual firing chamber, and in dual firing chamber, pass into air by the first blower fan, making the oxygen supply in pyrocrack furnace more abundant, efficiency of combustion is higher.
4, the arc mesh cap structure above the bottom ajutage adopted bottom main combustion chamber of the present invention and pipe, it is simple to rubbish ventilation oxygen supply is burnt, and avoids ashes to block simultaneously.
Accompanying drawing explanation
Fig. 1 is left view perspective view of the present invention.
Fig. 2 is that perspective view is looked on the right side of the present invention.
Fig. 3 is A place close-up schematic view in Fig. 1.
Fig. 4 is schematic front view in Fig. 1.
Fig. 5 is schematic top plan view in Fig. 1.
Fig. 6 is internal sectional perspective view of the present invention.
Fig. 7 is B place close-up schematic view in Fig. 6.
Fig. 8 is part body of heater cavity cross-sectional schematic in Fig. 2.
Fig. 9 is blast cap and bottom ajutage fit structure schematic diagram.
Described in figure, label character is expressed as: 1, body of heater; 101, main combustion chamber; 102, blast cap; 103, lower floor's observation window; 104, fume emission mouth; 2, condensation chamber; 3, dual firing chamber; 4, afterheat generating system; 5, blower system; 6, Separate System of Water-jet; 7, residual neat recovering system;
201, side plate; 202, flue gas dividing plate; 203, heat-insulation chamber; 204, swash plate;
301, swash plate; 302, air vent;
401, the first waste heat recovery oil tank; 402, the second waste heat recovery oil tank; 403, oil pipe;
501, the first blower fan; 502, the first air main; 503, sidewall air supply pipe; 511, the second blower fan; 512, the second air main; 513, air-supply intervalve; 514, bottom ajutage;
601, overflow pipe; 602, upper strata observation panel; 603, upper strata conveying pipe; 604, moisture trap; 605, transfer tube; 606, smoke extracting tube; 607, trap; 608, draining intervalve; 609, drain pipe;
701, waste heat water pipe; 702, waterpipe jointing; 703, the fixing seat of water pipe.
Detailed description of the invention
In order to make those skilled in the art be more fully understood that technical scheme, describing the present invention below in conjunction with accompanying drawing, the description of this part is only exemplary and explanatory, and protection scope of the present invention should not have any restriction effect.
As shown in Fig. 1-Fig. 7, the concrete structure of the present invention is: a kind of efficiently short cracking dual firing chamber rubbish thermal cracking heat energy reburner, and it includes body of heater 1, and it is internally provided with main combustion chamber 101, is provided above dog-house and stove cover plate;Described body of heater inner chamber surrounding is hollow interlayer structure, and interlayer is divided into two-layer blocked up and down, is provided above as the condensation chamber 2 of steam cooling in stove, and lower section is the dual firing chamber 3 connected with main combustion chamber 101; Arranged outside at condensation chamber 2 has the Separate System of Water-jet 6 bottom connection condensation chamber 2; The bottom of described body of heater 1 is provided with afterheat generating system 4, and described body of heater 1 side and bottom are connected to blower system 5, and the right side of body of heater 1 is provided with fume emission mouth 104;
Described afterheat generating system 4 includes the first waste heat recovery oil tank 401 being arranged on the bottom of body of heater 1 and the second waste heat recovery oil tank 402 being arranged on body of heater 1 sidepiece; And first waste heat recovery oil tank 401 and the second waste heat recovery oil tank 402 be connected to TRT by oil pipe 403.
As shown in Figs. 7-8, preferably, described condensation chamber 2 includes and the side plate 201 of body of heater 1 inwall formation air inlet, and condensation chamber 2 is internal is provided with some S shape flues by flue gas dividing plate 202, and is connected with the Separate System of Water-jet 6 of outside distribution below condensation chamber 2.
As shown in Figure 8, it is preferred that flue gas dividing plate 202 horizontally set of described condensation chamber 2, and the both sides of condensation chamber 2 are provided with heat-insulation chamber 203, condensation chamber 2 be arranged below outward-dipping swash plate 204.
As shown in Figure 1, shown in Figure 5, preferably, described Separate System of Water-jet 6 includes the overflow pipe 601 being connected to bottom condensation chamber 2, and each overflow pipe 601 is communicated on the upper strata conveying pipe 603 of body of heater 1 arranged outside, and upper strata conveying pipe 603 passes on left trap 607 and is connected to drain pipe 9; Connecting the upper end of gas and water separator 604 on the right side of upper strata conveying pipe 603, gas and water separator 604 bottom is connected to drain pipe 609, and the upper end opposite side of gas and water separator 604 connects the second blower fan 511 of blower system 5 by smoke extracting tube 606.
As shown in Figure 4, it is preferred that the trap 607 on the left of described upper strata conveying pipe 603 carries the draining intervalve 608 of pipe 603 to be connected to drain pipe 9 by vertically height lower than upper strata, and the vertically height of drain pipe 9 is lower than the height of draining intervalve 608; The transfer tube 605 of elbow-shaped it is connected between upper end and the smoke extracting tube 606 of described gas and water separator 604.
As shown in Figure 3, Figure 4, it is preferred that described overflow pipe 601 end faces outwards is provided with upper strata observation panel 602, and overflow pipe 601 be connected with upper strata conveying pipe 603 by the connecting tube being arranged below.
As shown in Figure 2, it is preferred that, described blower system 5 includes the first blower fan 501, the first air main 502 being connected with the first blower fan 501, and the first air main 502 is linked into the side bottom of body of heater 1 by the sidewall air supply pipe 503 that body of heater 1 both sides are arranged; Several spaced bottom ajutages 514 that the air inlet of the second blower fan 511 is arranged below with body of heater 1 are connected.
Preferably, described dual firing chamber 3 is connected with main combustion chamber 101 by the hole of polylith swash plate 301 interval composition near the side of body of heater 1 inner chamber; And sidewall air supply pipe 503 is connected to the air vent 302 arranged bottom dual firing chamber 3. By Fig. 8 it will be seen that swash plate 301 is elongate configuration, its spaced composition is shutter, and swash plate 301 be oriented from bottom to top, hole is internal towards dual firing chamber 3 obliquely.
Preferably, described second blower fan 511 is communicated to bottom ajutage 514 by the second air main 512 and the air-supply intervalve 513 that is connected with the second air main 512; Described bottom ajutage 514 is communicated to bottom in body of heater 1, and is covered with above it for ventilated arc mesh blast cap 102.
Preferably, described dual firing chamber 3 is internally provided with residual neat recovering system 7, described residual neat recovering system 7 includes being arranged in the waste heat water pipe 701 that the S shape within dual firing chamber 3 is arranged, and the fixing seat 703 of water pipe for fixing waste heat water pipe 701, and supplied water with outer loop by the waterpipe jointing 702 arranged in the left hand external of body of heater 1.
Time specifically used, rubbish is poured in main combustion chamber 101 from the top of body of heater 1, the rubbish loaded in main combustion chamber 101 is higher than swash plate 301, namely rubbish to be completely covered the residing height of swash plate 301, so that the alkane gas physical ability that the rubbish in stove produces due to pyrolysis is burnt completely in dual firing chamber 3; Simultaneously as the bottom of dual firing chamber 3 is connected to steam line, the rubbish bottom in pyrocrack furnace is also made to have the oxygen supply of abundance so that rubbish is soft is easy to burning.
The convenient steam collected in stove of the condensation chamber of pyrocrack furnace inner upper, it is simple to the later stage processes; Adopt Separate System of Water-jet simultaneously, by tail gas again with.
And the tail gas in the condenser system of upper strata is passed into bottom pyrocrack furnace by the air supply duct of bottom again, containing partial oxidation and fuel gas in tail gas, fuel gas burns again, and oxygen makes full use of oxygen supply, promotes the abundant pyrolysis of rubbish in main combustion chamber 101.
And the residual neat recovering system 7 arranged in dual firing chamber 3, including the waste heat water pipe 701 of S shape and the fixing seat 703 of water pipe, by outside waterpipe jointing 702 periodical feeding, take away the calory burning within dual firing chamber 3, make full use of heat energy.
Adopt a kind of efficient short cracking dual firing chamber of present invention rubbish thermal cracking heat energy reburner, optimize air blast ventilation channel, promote that rubbish fully burns, minimizing exhaust emissions, and make full use of the waste heat of pyrocrack furnace, the hot efficiency of combustion of gain of heat pyrolysis furnace.
It should be noted that, in this article, term " includes ", " comprising " or its any other variant are intended to comprising of nonexcludability, so that include the process of a series of key element, method, article or equipment not only include those key elements, but also include other key elements being not expressly set out, or also include the key element intrinsic for this process, method, article or equipment.
Principles of the invention and embodiment are set forth by specific case used herein, and the explanation of above example is only intended to help to understand method and the core concept thereof of the present invention. The above is only the preferred embodiment of the present invention, should be understood that, finiteness due to literal expression, and objectively there is unlimited concrete structure, for those skilled in the art, under the premise without departing from the principles of the invention, it is also possible to make some improvement, retouching or change, it is also possible to above-mentioned technical characteristic is combined by rights; These improve retouching, change or combination, or the not improved design by invention and technical scheme directly apply to other occasion, are regarded as protection scope of the present invention.
Claims (10)
1. an efficiently short cracking dual firing chamber rubbish thermal cracking heat energy reburner, it includes body of heater (1), and it is internally provided with main combustion chamber (101), is provided above dog-house and stove cover plate; It is characterized in that, described body of heater inner chamber surrounding is hollow interlayer structure, and interlayer is divided into two-layer blocked up and down, being provided above as the condensation chamber (2) of steam cooling in stove, lower section is the dual firing chamber (3) connected with main combustion chamber (101);Arranged outside at condensation chamber (2) has the Separate System of Water-jet (6) of connection condensation chamber (2) bottom; The bottom of described body of heater (1) is provided with afterheat generating system (4), described body of heater (1) side and bottom are connected to blower system (5), and the right side of body of heater (1) is provided with fume emission mouth (104);
Described afterheat generating system (4) includes the first waste heat recovery oil tank (401) being arranged on the bottom of body of heater (1) and the second waste heat recovery oil tank (402) being arranged on body of heater (1) sidepiece; And first waste heat recovery oil tank (401) and the second waste heat recovery oil tank (402) be connected to TRT by oil pipe (403).
2. one according to claim 1 efficiently short cracking dual firing chamber rubbish thermal cracking heat energy reburner, it is characterized in that, described condensation chamber (2) includes and the side plate (201) of body of heater (1) inwall formation air inlet, condensation chamber (2) is internal is provided with some S shape flues by flue gas dividing plate (202), and condensation chamber (2) lower section is connected with the Separate System of Water-jet (6) of outside distribution.
3. one according to claim 2 efficiently short cracking dual firing chamber rubbish thermal cracking heat energy reburner, it is characterized in that, flue gas dividing plate (202) horizontally set of described condensation chamber (2), and the both sides of condensation chamber (2) are provided with heat-insulation chamber (203), condensation chamber (2) be arranged below outward-dipping swash plate (204).
4. one according to claim 1 efficiently short cracking dual firing chamber rubbish thermal cracking heat energy reburner, it is characterized in that, described Separate System of Water-jet (6) includes the overflow pipe (601) being connected to condensation chamber (2) bottom, each overflow pipe (601) is communicated on upper strata conveying pipe (603) of body of heater (1) arranged outside, and upper strata conveying pipe (603) passes on left trap (607) and is connected to drain pipe (9); Right side, upper strata conveying pipe (603) connects the upper end of gas and water separator (604), gas and water separator (604) bottom is connected to drain pipe (609), and the upper end opposite side of gas and water separator (604) connects second blower fan (511) of blower system (5) by smoke extracting tube (606).
5. one according to claim 4 efficiently short cracking dual firing chamber rubbish thermal cracking heat energy reburner, it is characterized in that, the trap (607) in left side, described upper strata conveying pipe (603) is connected to drain pipe (9) by vertically height lower than the draining intervalve (608) on upper strata conveying pipe (603), and the vertically height of drain pipe (9) is lower than the height of draining intervalve (608); The transfer tube (605) of elbow-shaped it is connected between upper end and the smoke extracting tube (606) of described gas and water separator (604).
6. one according to claim 4 efficiently short cracking dual firing chamber rubbish thermal cracking heat energy reburner, it is characterized in that, described overflow pipe (601) end faces outwards is provided with upper strata observation panel (602), and overflow pipe (601) is connected with upper strata conveying pipe (603) by the connecting tube being arranged below.
7. one according to claim 1 efficiently short cracking dual firing chamber rubbish thermal cracking heat energy reburner, it is characterized in that, described blower system (5) includes the first blower fan (501), the first air main (502) being connected with the first blower fan (501), and the first air main (502) is linked into the side bottom of body of heater (1) by the sidewall air supply pipe (503) that body of heater (1) both sides are arranged; Several spaced bottom ajutages (514) that the air inlet of the second blower fan (511) is arranged below with body of heater (1) are connected.
8. one according to claim 7 efficiently short cracking dual firing chamber rubbish thermal cracking heat energy reburner, it is characterized in that, described dual firing chamber (3) is connected with main combustion chamber (101) by the hole of polylith swash plate (301) interval composition near the side of body of heater (1) inner chamber;And sidewall air supply pipe (503) is connected to the air vent (302) that dual firing chamber (3) bottom is arranged.
9. one according to claim 7 efficiently short cracking dual firing chamber rubbish thermal cracking heat energy reburner, it is characterized in that, described second blower fan (511) is communicated to bottom ajutage (514) by the second air main (512) and the air-supply intervalve (513) that is connected with the second air main (512); Described bottom ajutage (514) is communicated to body of heater (1) interior bottom, and is covered with above it for ventilated arc mesh blast cap (102).
10. one according to claim 1 efficiently short cracking dual firing chamber rubbish thermal cracking heat energy reburner, it is characterized in that, described dual firing chamber (3) is internally provided with residual neat recovering system (7), described residual neat recovering system (7) includes being arranged in the waste heat water pipe (701) that the internal S shape of dual firing chamber (3) is arranged, and the fixing seat (703) of water pipe being used for fixing waste heat water pipe (701), and supplied water with outer loop by the waterpipe jointing (702) arranged in the left hand external of body of heater (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521064380.1U CN205316331U (en) | 2015-12-17 | 2015-12-17 | High -efficient short schizolysis second combustion chamber rubbish thermal cracking heat energy reborner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521064380.1U CN205316331U (en) | 2015-12-17 | 2015-12-17 | High -efficient short schizolysis second combustion chamber rubbish thermal cracking heat energy reborner |
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| Publication Number | Publication Date |
|---|---|
| CN205316331U true CN205316331U (en) | 2016-06-15 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521064380.1U Withdrawn - After Issue CN205316331U (en) | 2015-12-17 | 2015-12-17 | High -efficient short schizolysis second combustion chamber rubbish thermal cracking heat energy reborner |
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| CN (1) | CN205316331U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105444181A (en) * | 2015-12-17 | 2016-03-30 | 刘安桂 | Two-combustion-chamber garbage thermal cracking heat energy conversion furnace for efficiently accelerating cracking |
-
2015
- 2015-12-17 CN CN201521064380.1U patent/CN205316331U/en not_active Withdrawn - After Issue
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105444181A (en) * | 2015-12-17 | 2016-03-30 | 刘安桂 | Two-combustion-chamber garbage thermal cracking heat energy conversion furnace for efficiently accelerating cracking |
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