CN102374545A - Heat-storage incinerator - Google Patents
Heat-storage incinerator Download PDFInfo
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- CN102374545A CN102374545A CN2010102544613A CN201010254461A CN102374545A CN 102374545 A CN102374545 A CN 102374545A CN 2010102544613 A CN2010102544613 A CN 2010102544613A CN 201010254461 A CN201010254461 A CN 201010254461A CN 102374545 A CN102374545 A CN 102374545A
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Abstract
The invention discloses a heat-storage incinerator, which is characterized in that: a plurality of heat storage plates are filled inside a first heat storage bed and a second heat storage bed, which can be alternative to connect and disconnect, wherein a burner is arranged between the first heat storage bed and the second heat storage bed, two ends of a circulating burning pipeline are respectively communicated with an inlet end and an outlet end of the burner, a first outlet end and a second outlet end of an airflow distribution chamber are arranged on the bottom part of the airflow distribution chamber and are respectively communicated with the first heat storage bed and the second heat storage bed, the first outlet end and the second outlet end of the airflow distribution chamber are respectively provided with a movable valve, the two movable valves can be alternatively selected to open and close the first outlet end and the second outlet end, at least an airflow passage is arranged between the airflow distribution chamber and the circulating burning pipeline, and a passage switch capable of controlling the opening and the closing of the airflow passage is arranged inside the airflow passage. A burning gas of the circulating burning pipeline can be used as a driving force to propel the residual waste gas inside the airflow distribution chamber and pipelines into the heat storage beds so as to be thermally decomposed, so the problems such as the residual gas and the leakage can be solved.
Description
Technical field
The present invention relates to a kind of incinerator, particularly a kind of can with in its equipment or the pipeline the waste gas of residual VOC make the heat accumulating type incinerator effectively handled.
Background technology
In life with in the procedure for producing of various industry, can use many have volatile solvent or petrochemical industry oil products usually; For example gasoline, paint, cleaning agent, seccotine, sticker, solvent, oil product, petrochemical material etc.; These solvents then can form harmful exhaust and be spread in the air after volatilization; This be VOC (Volatile Organic Compounds, VOCs).
In the known general adhesive tape processing procedure, be that organic solvent is added in the sticker, and coat again on the different base materials in normal temperature dilution allotment; For example on polyvinyl chloride (PVC), polyethylene (PE), cloth, composite and the glass stationery, through the baking oven heated baking, again with organic solvent evaporation; Make the dry top layer and the base material of fitting fully of forming of sticker, process adhesive tape through processed again, yet; In the aforesaid adhesive tape procedure for producing, will supervene a large amount of volatile organic compound from waste gas.
VOC can produce great harm to health; Short-time contact gently then makes human body not feel well; Produce dizzy, feel sick, vomit, shed tears, be pungent, symptom such as cough; Can cause during excessive concentration being poisoned to death, can cause diseases such as liver, lung, respiratory tract when contacting for a long time, very the person more can cause the human carcinogen.In addition,,, thereby have easy aptitude to burn again because of its volatilization point pole own is low because its composition of VOC all has carbon, protium, when the VOC excessive concentration, the harm of then blasting easily Yu burning.Therefore VOC such as unprocessed directly is disposed to atmosphere then can influence health, produce danger and also influence environmental quality, just can be disposed in the atmosphere after must dealing carefully with.
Utilizing incinerator to handle VOC is the processing method of a high efficiency and environmental protection, and it is suitably being operated under the incineration condition, and then the clearance of VOC can be up to more than 99%.Heat accumulating type incinerator (Regenerative thermal oxidizer; RTO) be the principle of utilizing high-temperature oxydation; Volatility organic volatile property organic compound that various industrial process produced under enough temperature and reaction time, is resolved into steam and carbon dioxide via heating, again it is discharged in the atmosphere; And the high heat that oxidation produced carried out Waste Heat Recovery with regenerative apparatus, with the required heat energy firing rate of reduction system.
Existing heat accumulating type incinerator disposes two energy storage beds usually; And all be filled with some ceramic heat-storing plates in the energy storage bed; Because the ceramic heat-storing plate has high heat storage capacity and large contact surface is long-pending; Make that when its waste gas of VOC was flowed through heat accumulation plate, organic solvent contained in the waste gas resolved into steam and carbon dioxide via high-temperature oxydation; Incidental branch is analgesic when incinerating simultaneously can be stored accumulation of heat again in through another group energy storage bed the time; Use as reclaiming heat energy; So switch burning and accumulation of heat alternately via two energy storage beds; Its heat recovery efficiency can not only can reach the purpose of effective processing VOC up to more than 95%, can reduce the operation of equipment cost greatly again simultaneously.
Yet; Heat accumulating type incinerator is when the burning of two energy storage beds and accumulation of heat switching or blowing out; Pending waste gas takes place and also is not able to do in time to be stranded in equipment or the pipeline through energy storage bed in regular meeting, therefore can have periodically residual untreated exhaust gas, like this; When heat accumulating type incinerator switches at each valve member, just have the problem of remaining untreated pollution from exhaust emission and leakage.
Summary of the invention
In order to remedy above deficiency, the invention provides a kind of heat accumulating type incinerator, this heat accumulating type incinerator can be pushed into residual waste gas in gas distribution chamber and the pipeline and carry out thermal decomposition in the energy storage bed, can solve problems such as residual gas and leakage.
The present invention for the technical scheme that solves its technical problem and adopt is: a kind of heat accumulating type incinerator; Comprise first and second energy storage bed; This first and second alternative break-make of energy storage bed connects (phenomenon of adverse current or mixed flow taking place to each other to avoid gas in first and second energy storage bed); First and second energy storage bed inside filling respectively is provided with several heat accumulation plates; Be provided with a burner between this first and second energy storage bed, be provided with burning gases (these burning gases provide the heat accumulation plate accumulation of heat of thermal source to first and second energy storage bed) in the burner; Also be provided with a circulating combustion pipeline, these circulating combustion pipeline two ends are communicated in the import and export end of burner respectively, and the burning gases in the burner circulate in the circulating combustion pipeline; Also be provided with a gas distribution chamber; This gas distribution chamber is provided with an entrance point and first and second port of export; To use direction to be benchmark, this first and second port of export is positioned at this gas distribution chamber bottom and is connected with first and second energy storage bed through pipeline respectively, is arranged with a Movable valve on first and second port of export of gas distribution chamber again; These two Movable valves can switch the keying of selecting first and second port of export each other, and then which energy storage bed of gas flow of being sent into by entrance point of decision; Gas distribution chamber is provided with gas channel at least with between the circulating combustion pipeline again; Be provided with a channel switch in this gas channel; This channel switch can be controlled the logical of gas channel and close, and behind the air intake inflow gas distribution chamber of the waste gas with VOC via incinerator, utilizes the switching of the Movable valve of gas distribution chamber that waste gas is flowed in first energy storage bed; This moment, first energy storage bed can be with the complete heating and decomposition of this waste gas; Make the gas of handling through second energy storage bed again, supply the heat accumulation plate in second energy storage bed to accumulate heat energy, the gas after the processing gives off the external world immediately; When incinerator is shut down; Gas distribution chamber and with the pipeline of energy storage bed in will residual a large amount of waste gas; Only need open the gas channel of gas distribution chamber and circulating combustion pipeline this moment, and this distribution of air flow of burning gases importing that circulates is indoor, utilizes the power of gas; With in gas distribution chamber and the pipeline thereof residual waste gas push first and second energy storage bed to, the heat energy that utilizes first and second energy storage bed to accumulate carries out thermal decomposition.
As further improvement of the present invention; The structure that said two Movable valves can switch the keying of selecting first and second port of export each other is: the Movable valve of said first and second port of export of gas distribution chamber is respectively first and second cylinder; Be respectively equipped with first and second baffle plate on piston rod one end of this first and second cylinder; This first and second baffle plate can seal first and second port of export of gas distribution chamber respectively; When first and second cylinder action, it is flexible that its inner compressed air will promote its piston rod, and pass through the keying of first and second port of export of first and second baffle controls gas distribution chamber on the piston rod.
As further improvement of the present invention; Gas distribution chamber is respectively equipped with one deck internal partition and one deck external partition on its bottom; And be formed with two first and second perforation on this inside and outside dividing plate respectively; First and second punch position on this inside and outside dividing plate is corresponding one by one; Said cylinder piston rod overhead gage is between the inside and outside dividing plate of gas distribution chamber, and this baffle plate is corresponding to first and second perforation on the inside and outside dividing plate, and the external diameter of baffle plate is greater than the internal diameter of first and second perforation on the inside and outside dividing plate; Thereby the piston rod of first and second cylinder drives the flexible keying of controlling first and second perforation on the inside and outside dividing plate of first and second baffle plate, and then which energy storage bed decision waste gas sends into by which port of export of gas distribution chamber; When the second perforation sealing of first baffle plate of first cylinder with external partition; The second baffle of second cylinder then discharges the perforation of first on the internal partition; When waste gas is got into by the entrance point of gas distribution chamber; Just can flow into the mezzanine space between this distribution of air flow indoor and outdoor dividing plate, further second port of export bottom gas distribution chamber and pipeline are sent to and carry out thermal decomposition process in second energy storage bed; Discharge second perforation of external partition when first baffle plate of first cylinder; And first perforation on the second baffle of second cylinder sealing internal partition; When then waste gas is got into by the entrance point of gas distribution chamber, just can be sent to through pipeline and carry out thermal decomposition process in first energy storage bed through the port of export bottom second perforation and the gas distribution chamber; Aforementioned two kinds of air-flow travel paths can effectively utilize first and second energy storage bed independent process waste gas respectively; And when first energy storage bed carries out exhaust-gas treatment; Its waste gas of handling will flow in second energy storage bed again; Accumulated behind the heat energy and given off the external world immediately by its inner heat accumulation plate, vice versa uses second energy storage bed to carry out exhaust-gas treatment, and first energy storage bed is as the usefulness of accumulation of heat; This waste gas is after heat treated finishes in first and second energy storage bed, outputs to the external world by the floss hole of the accumulation of heat port of export of first and second energy storage bed.
As further improvement of the present invention; The structure that the alternative break-make of first and second energy storage bed connects is: be provided with the passage that is interconnected between first and second energy storage bed; Be provided with a control valve in this passage; The break-make of this control valve controllable channel, thus whether the passage of controlling between first and second energy storage bed is communicated with, and to avoid gas in each energy storage bed the phenomenon of adverse current or mixed flow takes place to each other.
As further improvement of the present invention; Be provided with a fan in the said circulating combustion pipeline; Wind-force circulating combustion gas through fan; These burning gases are constantly circulated in pipeline, fan is set after the circulating combustion pipeline have the splendid thermal efficiency, and can prevent effectively that heat energy dissipation from going out the external world.
As further improvement of the present invention; Be provided with a heat exchanger in the said circulating combustion pipeline; These heat exchanger two ends are respectively equipped with an oil-in and an oil-out, and the cold oil of normal temperature injects from oil-in, then with this circulating combustion pipeline in the high hot combustion gas that circulates carry out a heat exchange procedure; Just obtain deep fat then, can be used for the adhesive tape heating processing procedures by the oil-out place of this heat exchanger.
As further improvement of the present invention; The logical structure of closing that channel switch can be controlled gas channel is: said channel switch is the disk shape; This channel switch external diameter is consistent with gas channel internal diameter size; This channel switch is articulated in the gas channel, can control air flow rate size and break-make in the gas channel through regulating disk shape channel switch.
As further improvement of the present invention, the inner heat accumulation plate of said first and second energy storage bed is not the ceramic heat-storing plate, and the ceramic heat-storing plate can be accumulated heat energy and make first and second energy storage bed maintain under the fixing high temperature, and influenced by ambient temperature and lower the temperature.
As further improvement of the present invention, be provided with the twice gas channel between gas distribution chamber and circulating combustion pipeline, be equipped with a channel switch in the per pass gas channel.
The invention has the beneficial effects as follows: the present invention is communicated with the circulating combustion pipeline gas distribution chamber through a gas channel; In gas channel, be provided with its logical channel switch that closes of control; Like this with regard to the burning gases of this circulating combustion pipeline capable of using as a motive force; Can residual waste gas in gas distribution chamber and the pipeline be pushed into and carry out thermal decomposition in the energy storage bed, and then can solve problems such as residual gas and leakage.
Description of drawings
Fig. 1 is first stereogram of the present invention;
Fig. 2 is the vertical view of Fig. 1;
Fig. 3 is second stereogram of the present invention;
Fig. 4 is first kind of working state schematic representation of the present invention;
Fig. 5 moves towards thin portion sketch map for first kind of duty waste gas of the present invention;
Fig. 6 is second kind of working state schematic representation of the present invention.
The specific embodiment
Embodiment: a kind of heat accumulating type incinerator; Comprise first and second energy storage bed 101,102; These first and second energy storage bed 101,102 alternative break-makes connect (phenomenon of adverse current or mixed flow taking place to each other to avoid first and second energy storage bed 101,102 interior gases); First and second energy storage bed 101,102 inside filling respectively are provided with several heat accumulation plates; This 101,102 of first and second energy storage bed is provided with a burner 11, is provided with burning gases (these burning gases provide the heat accumulation plate accumulation of heat of thermal source to first and second energy storage bed) in the burner 11; Also be provided with a circulating combustion pipeline 20, these circulating combustion pipeline 20 two ends are communicated in the import and export end of burner 11 respectively, and the burning gases in the burner 11 circulate in circulating combustion pipeline 20; Also be provided with a gas distribution chamber 30; This gas distribution chamber 30 is provided with an entrance point 31 and first and second port of export 321,322; To use direction to be benchmark; This first and second port of export 321,322 is positioned at these gas distribution chamber 30 bottoms and is connected with first and second energy storage bed 101,102 through pipeline respectively; Be arranged with a Movable valve on first and second port of export 321,322 of gas distribution chamber 30 again, these two Movable valves can switch the keying of selecting first and second port of export 321,322 each other, and then which energy storage bed of gas flow of being sent into by entrance point 31 of decision; Gas distribution chamber 30 is provided with gas channel 35 at least with 20 of circulating combustion pipelines again; Be provided with a channel switch 351 in this gas channel 35; This channel switch 351 can be controlled the logical of gas channel 35 and close, and behind the air intake 40 inflow gas distribution chambers 30 of the waste gas with VOC via incinerator, utilizes the switching of the Movable valve of gas distribution chamber 30 that waste gas is flowed in first energy storage bed 101; This moment, first energy storage bed 101 can be with the complete heating and decomposition of this waste gas; Make the gas of handling through second energy storage bed 102 again, supply the heat accumulation plates in second energy storage bed 102 to accumulate heat energy, the gas after the processing gives off the external world immediately; When incinerator is shut down; Gas distribution chamber 30 and with the pipeline of energy storage bed in will residual a large amount of waste gas; Only need this moment the gas distribution chamber 30 and the gas channel 35 of circulating combustion pipeline 20 are opened, and the burning gases that circulate are imported in this gas distribution chamber 30, utilize the power of gas; With in gas distribution chamber 30 and the pipeline thereof residual waste gas push first and second energy storage bed 101,102 to, the heat energy that utilizes first and second energy storage bed 101,102 to accumulate carries out thermal decomposition.
The structure that said two Movable valves can switch the keying of selecting first and second port of export 321,322 each other is: the Movable valve of said gas distribution chamber 30 first and second ports of export 321,322 is respectively first and second cylinder 341,342; Be respectively equipped with first and second baffle plate 343,344 on piston rod one end of this first and second cylinder 341,342; This first and second baffle plate 343,344 can seal first and second port of export 321,322 of gas distribution chamber 30 respectively; When first and second cylinder 341,342 actions; It is flexible that its inner compressed air will promote its piston rod, and control the keying of first and second port of export 321,322 of gas distribution chambers 30 through first and second baffle plate 343,344 on the piston rod.
Said gas distribution chamber is respectively equipped with one deck internal partition 33A and one deck external partition 33B on 30 its bottoms; And this inside and outside dividing plate 33A, 33B be last to be formed with two first and second perforation 331,332 respectively; This inside and outside dividing plate 33A, first and second last 331,332 positions correspondence one by one of boring a hole of 33B; Said cylinder piston rod overhead gage is between the inside and outside dividing plate 33A of gas distribution chamber 30,33B; This baffle plate is corresponding to inside and outside dividing plate 33A, first and second last perforation 331,332 of 33B; And the external diameter of baffle plate is greater than the internal diameter of first and second last perforation 331,332 of inside and outside dividing plate 33A, 33B; Thereby the piston rod of first and second cylinder 341,342 drives the flexible keying of controlling first and second last perforation 331,332 of inside and outside dividing plate 33A, 33B of first and second baffle plate 343,344, and then which energy storage bed decision waste gas sends into by which port of export of gas distribution chamber 30; When second perforation, 332 sealings of first baffle plate 343 of first cylinder 341 with external partition 33B; The second baffle 344 of second cylinder 342 then discharges the perforation of first on the internal partition 33A 331; When waste gas is got into by the entrance point of gas distribution chamber 30 31; Just can flow into the mezzanine space between this gas distribution chamber 30 inside and outside dividing plate 33A, 33B, further second port of export 322 through gas distribution chamber 30 bottoms and pipeline are sent in second energy storage bed 102 and carry out thermal decomposition process; Discharge second perforation 332 of external partition 33B when first baffle plate 343 of first cylinder 341; And first perforation 331 on the second baffle 344 sealing internal partition 33A of second cylinder 342; When then waste gas is got into by the entrance point of gas distribution chamber 30 31, just can through second bore a hole 332 and the port of export of gas distribution chamber 30 bottoms be sent in first energy storage bed 101 through pipeline and carry out thermal decomposition process; Aforementioned two kinds of air-flow travel paths can effectively utilize first and second energy storage bed 101,102 independent process waste gas respectively; And when first energy storage bed 101 carries out exhaust-gas treatment; Its waste gas of handling will flow in second energy storage bed 102 again; Accumulated behind the heat energy and given off the external world immediately by its inner heat accumulation plate, vice versa uses second energy storage bed 102 to carry out exhaust-gas treatment, and first energy storage bed 101 is as the usefulness of accumulation of heat; This waste gas is after heat treated finishes in first and second energy storage bed 101,102, outputs to the external world by the floss hole 411 of the accumulation of heat port of export 41 of first and second energy storage bed 101,102.
The structure that said first and second energy storage bed 101,102 alternative break-makes connect is: first and second energy storage bed 101, be provided with the passage that is interconnected between 102; Be provided with a control valve in this passage; The break-make of this control valve controllable channel; Thereby control first and second energy storage bed 101, whether the passage between 102 is communicated with, the phenomenon of adverse current or mixed flow takes place to each other to avoid gas in each energy storage bed.
Be provided with a fan in the said circulating combustion pipeline 20; Wind-force circulating combustion gas through fan; These burning gases are constantly circulated in pipeline, fan is set after circulating combustion pipeline 20 have the splendid thermal efficiency, and can prevent effectively that heat energy dissipation from going out the external world.
Be provided with a heat exchanger 21 in the said circulating combustion pipeline 20; These heat exchanger 21 two ends are respectively equipped with an oil-in 211 and an oil-out 212; The cold oil of normal temperature injects from oil-in 211; Then with this circulating combustion pipeline 20 in high hot combustion gas of circulation carry out a heat exchange procedure, just obtain deep fat then by oil-out 212 places of this heat exchanger 21, can be used for the adhesive tape heating processing procedures.
The logical structure of closing that said channel switch 351 can be controlled gas channel 35 is: said channel switch 351 is the disk shape; These channel switch 351 external diameters are consistent with gas channel 35 internal diameters size; This channel switch 351 is articulated in the gas channel 35, can control air flow rate size and break-make in the gas channel 35 through regulating disk shape channel switch 351.
Said first and second energy storage bed 101,102 inner heat accumulation plates are not the ceramic heat-storing plate, and the ceramic heat-storing plate can be accumulated heat energy and make first and second energy storage bed 101,102 maintain under the fixing high temperature, and influenced by ambient temperature and lower the temperature.
20 of said gas distribution chamber 30 and circulating combustion pipelines are provided with twice gas channel 35, are equipped with a channel switch 351 in the per pass gas channel 35.
Claims (9)
1. heat accumulating type incinerator; Comprise first and second energy storage bed (101,102); The alternative break-make of this first and second energy storage bed (101,102) connects; First and second energy storage bed (101,102) inside filling respectively is provided with several heat accumulation plates, and this first and second energy storage bed is provided with a burner (11) between (101,102), and burner is provided with burning gases in (11); Also be provided with a circulating combustion pipeline (20), these circulating combustion pipeline (20) two ends are communicated in the import and export end of burner (11) respectively, and the burning gases in the burner (11) circulate in circulating combustion pipeline (20); It is characterized in that: also be provided with a gas distribution chamber (30); This gas distribution chamber (30) is provided with an entrance point (31) and first and second port of export (321,322); To use direction to be benchmark; This first and second port of export (321,322) is positioned at this gas distribution chamber (30) bottom and is connected with first and second energy storage bed (101,102) through pipeline respectively; Be arranged with a Movable valve on first and second port of export of gas distribution chamber (30) (321,322) again, these two Movable valves can switch the keying of selecting first and second port of export (321,322) each other; Gas distribution chamber (30) is provided with gas channel (35) at least with between circulating combustion pipeline (20) again, is provided with a channel switch (351) in this gas channel (35), and this channel switch (351) can be controlled logical the closing of gas channel (35).
2. heat accumulating type incinerator according to claim 1; It is characterized in that: the structure that said two Movable valves can switch the keying of selecting first and second port of export (321,322) each other is: the Movable valve of first and second port of export of said gas distribution chamber (30) (321,322) is respectively first and second cylinder (341,342); Be respectively equipped with first and second baffle plate (343,344) on piston rod one end of this first and second cylinder (341,342), this first and second baffle plate (343,344) can seal first and second port of export (321,322) of gas distribution chamber (30) respectively.
3. heat accumulating type incinerator according to claim 2; It is characterized in that: gas distribution chamber (30) is respectively equipped with one deck internal partition (33A) and one deck external partition (33B) on its bottom; And be formed with two first and second perforation (331,332) on this inside and outside dividing plate (33A, 33B) respectively; First and second perforation (331,332) position on this inside and outside dividing plate (33A, 33B) is corresponding one by one; Said cylinder piston rod overhead gage is positioned between the inside and outside dividing plate (33A, 33B) of gas distribution chamber (30); This baffle plate is corresponding to first and second perforation (331,332) on the inside and outside dividing plate (33A, 33B), and the external diameter of baffle plate is greater than the internal diameter of first and second perforation (331,332) on the inside and outside dividing plate (33A, 33B).
4. heat accumulating type incinerator according to claim 1; It is characterized in that: the structure that the alternative break-make of first and second energy storage bed (101,102) connects is: first and second energy storage bed is provided with the passage that is interconnected between (101,102); Be provided with a control valve in this passage, the break-make of this control valve controllable channel.
5. heat accumulating type incinerator according to claim 1 is characterized in that: be provided with a fan in the said circulating combustion pipeline (20).
6. heat accumulating type incinerator according to claim 1 is characterized in that: be provided with a heat exchanger (21) in the said circulating combustion pipeline (20), this heat exchanger (21) two ends are respectively equipped with an oil-in (211) and one fuel-displaced (212).
7. heat accumulating type incinerator according to claim 1; It is characterized in that: the logical structure of closing that channel switch (351) can be controlled gas channel (35) is: said channel switch (351) is the disk shape; This channel switch (351) external diameter is consistent with gas channel (35) internal diameter size, and this channel switch (351) is articulated in the gas channel (35).
8. heat accumulating type incinerator according to claim 1 is characterized in that: the inner heat accumulation plate of said first and second energy storage bed (101,102) is the ceramic heat-storing plate.
9. heat accumulating type incinerator according to claim 1 is characterized in that: be provided with twice gas channel (35) between gas distribution chamber (30) and circulating combustion pipeline (20), be equipped with a channel switch (351) in the per pass gas channel (35).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201010254461.3A CN102374545B (en) | 2010-08-12 | 2010-08-12 | Heat-storage incinerator |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201010254461.3A CN102374545B (en) | 2010-08-12 | 2010-08-12 | Heat-storage incinerator |
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| CN102374545A true CN102374545A (en) | 2012-03-14 |
| CN102374545B CN102374545B (en) | 2015-01-14 |
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0818654A2 (en) * | 1996-07-08 | 1998-01-14 | Norton Chemical Process Products Corporation | Horizontal regenerative thermal oxidizer unit |
| CN1188872A (en) * | 1996-04-04 | 1998-07-29 | 丰田自动车株式会社 | Double-end radiation tube burner system |
| JP2001241637A (en) * | 2000-03-02 | 2001-09-07 | Ishikawajima Harima Heavy Ind Co Ltd | Method and apparatus for confirming deodorizing performance of regenerative deodorizing furnace |
| CN1928432A (en) * | 2005-09-06 | 2007-03-14 | 超尊科技股份有限公司 | Heat recovery combustion furnace |
| CN101435580A (en) * | 2007-11-15 | 2009-05-20 | 华懋科技股份有限公司 | Thermal storage cremation furnace for storing press and cleaning |
| CN201748444U (en) * | 2010-08-12 | 2011-02-16 | 昆山巨闳机械科技有限公司 | Heat accumulating type incinerator |
-
2010
- 2010-08-12 CN CN201010254461.3A patent/CN102374545B/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1188872A (en) * | 1996-04-04 | 1998-07-29 | 丰田自动车株式会社 | Double-end radiation tube burner system |
| EP0818654A2 (en) * | 1996-07-08 | 1998-01-14 | Norton Chemical Process Products Corporation | Horizontal regenerative thermal oxidizer unit |
| JP2001241637A (en) * | 2000-03-02 | 2001-09-07 | Ishikawajima Harima Heavy Ind Co Ltd | Method and apparatus for confirming deodorizing performance of regenerative deodorizing furnace |
| CN1928432A (en) * | 2005-09-06 | 2007-03-14 | 超尊科技股份有限公司 | Heat recovery combustion furnace |
| CN101435580A (en) * | 2007-11-15 | 2009-05-20 | 华懋科技股份有限公司 | Thermal storage cremation furnace for storing press and cleaning |
| CN201748444U (en) * | 2010-08-12 | 2011-02-16 | 昆山巨闳机械科技有限公司 | Heat accumulating type incinerator |
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|---|---|
| CN102374545B (en) | 2015-01-14 |
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