CN203333601U - Waste-boiler-type gasification furnace - Google Patents
Waste-boiler-type gasification furnace Download PDFInfo
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- CN203333601U CN203333601U CN2013203696631U CN201320369663U CN203333601U CN 203333601 U CN203333601 U CN 203333601U CN 2013203696631 U CN2013203696631 U CN 2013203696631U CN 201320369663 U CN201320369663 U CN 201320369663U CN 203333601 U CN203333601 U CN 203333601U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/16—Combined cycle power plant [CCPP], or combined cycle gas turbine [CCGT]
- Y02E20/18—Integrated gasification combined cycle [IGCC], e.g. combined with carbon capture and storage [CCS]
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Abstract
The utility model discloses a waste-boiler-type gasification furnace. The waste-boiler-type gasification furnace comprises a first furnace body, a second furnace body, an upper part main spray nozzle and an upper part auxiliary spray nozzle, wherein the first furnace body is internally provided with a combustion chamber, a first waste boiler cooling chamber and a shock chilling chamber; the first waste boiler cooling chamber comprises a first radiation cooling chamber and a first convection cooling chamber; the top end of the first radiation cooling chamber is communicated with the bottom end of the combustion chamber; the bottom end of the first radiation cooling chamber is open; the bottom end of the first convection cooling chamber is communicated with the bottom end of the first radiation cooling chamber; the upper part of the first convection cooling chamber is provided with a gas outlet; the second furnace body is internally provided with a second waste boiler cooling chamber; the second waste boiler cooling chamber comprises a second radiation cooling chamber and a second convection cooling chamber; the top end of the second radiation cooling chamber is communicated with a gas outlet; the bottom end of the second convection cooling chamber is communicated with the bottom end of the second radiation cooling chamber. The waste-boiler-type gasification furnace has the advantages of higher heat efficiency, high carbon conversion rate, high gasification efficiency and the like.
Description
Technical field
The utility model relates to coalification Poly-generation gasification technology, especially relates to the gasification of IGCC and coal high concentration CO processed, relates more specifically to a kind of waste boiler type vapourizing furnace.
Background technology
The vapourizing furnace of traditional multi-nozzle structure has two types: the first type is, in the bottom of the straight length of vapourizing furnace, a plurality of nozzles are set, gas is up, lime-ash is descending along furnace wall, such vapourizing furnace, system flow is long, useless Cooker structure complexity, the cost of equipment is high, and in operational process, coal fluctuates when large and is prone to cinder notch and stops up; The second type is, on the top of the straight length of vapourizing furnace, a plurality of nozzles are set, and gas is descending, lime-ash is descending along furnace wall, and such vapourizing furnace mostly is chilling process technique, and in operational process, coal fluctuates when large, also is prone to cinder notch and stops up.In addition, the body of heater of traditional vapourizing furnace mostly is firebrick structure, and coal adaptability is poor, the coal of the high ash melting point that can not gasify.
And the coalification Poly-generation gasification technology for current IGCC and coal high concentration CO processed, adopts chilling process technique more, causes the calorific loss of large section after the latent heat Quench in high-temperature synthesis gas, causes the thermo-efficiency of whole system low.
The utility model content
The utility model is intended to one of solve the problems of the technologies described above at least to a certain extent.For this reason, a purpose of the present utility model is to propose a kind of waste boiler type vapourizing furnace, gasification efficiency, efficiency of carbon conversion and system thermal efficiency that described waste boiler type vapourizing furnace can improve.
To achieve these goals, according to the utility model proposes a kind of waste boiler type vapourizing furnace.Described waste boiler type vapourizing furnace comprises: the first body of heater, there is superposed combustion chamber in described the first body of heater, be positioned at the useless pot cooling room in first below described combustion chamber and be positioned at the shock chamber below the described first useless pot cooling room, the described first useless pot cooling room comprises the first radiant cooling room and around the first convection current cooling room of described the first radiant cooling room, the top of described the first radiant cooling room is communicated with the bottom of described combustion chamber, the open bottom end of described the first radiant cooling room, the bottom of described the first convection current cooling room is communicated with the bottom of described the first radiant cooling room, the top of described the first convection current cooling room is provided with air outlet, the second body of heater, there is the second useless pot cooling room in described the second body of heater, the described second useless pot cooling room comprises the second radiant cooling room and around the second convection current cooling room of described the second radiant cooling room, the top of described the second radiant cooling room is communicated with described air outlet, the bottom of described the second convection current cooling room is communicated with the bottom of described the second radiant cooling room, and the top of described the second convection current cooling room is provided with syngas outlet, the top main jet, described top main jet is located at the center on the top of described the first body of heater, described top main jet, for uperize, dried coal powder, main oxygen, combustion-supporting gas and inflammable gas in from the top of described combustion chamber to described combustion chamber, is provided with integrated igniting and flame detecting device in the main jet of described top, with the upper secondary nozzle, described upper secondary nozzle is located at the top of described the first body of heater, for the top from described combustion chamber to uperize, oxygen and dried coal powder in described combustion chamber.
According to waste boiler type vapourizing furnace of the present utility model, by the useless pot cooling room that two series connection are set, (be the described first useless pot cooling room and described second useless pot of cooling room series connection, and the described first useless pot cooling room and the described second useless pot cooling room all comprise radiant cooling room and convection current cooling room), latent heat in high-temperature synthesis gas can be by each radiant cooling room and the heat exchange of convection current cooling room in the described first useless pot cooling room and the described second useless pot cooling room, thereby can reclaim fully the latent heat of high-temperature gas, can improve heat recovery and utilization efficiency (thermo-efficiency of described waste boiler type vapourizing furnace can up to more than 90%).Described waste boiler type vapourizing furnace during for projects such as IGCC, coal high concentration CO processed, can make system thermal efficiency higher.
And, according to waste boiler type vapourizing furnace of the present utility model by described top main jet and described upper secondary nozzle are set, can increase the disturbance of the high-temperature gas in described waste boiler type vapourizing furnace, thereby what can make dried coal powder and vaporized chemical (such as main oxygen, combustion-supporting gas, inflammable gas, steam etc.) mix is more even, improve the charcoal transformation efficiency, increased the rate of decomposition of the gas forming amount of the dried coal powder of unit mass, effective gas composition and steam.Wherein, in dried coal powder, the transformation efficiency of charcoal can reach more than 99.5%, can improve significantly gasification efficiency.
In addition, by described top main jet and described upper secondary nozzle are set, thereby not only can regulate more easily the load of described waste boiler type vapourizing furnace, and can be amplified (volume that improves described waste boiler type vapourizing furnace) to described waste boiler type vapourizing furnace more easily.Therefore, have that thermo-efficiency is higher, efficiency of carbon conversion is high, gasification efficiency is high, be convenient to amplify, be convenient to regulate the advantage such as load according to waste boiler type vapourizing furnace of the present utility model.
In addition, according to the utility model, above-mentioned waste boiler type vapourizing furnace can also have following additional technical characterictic:
Described top main jet is the first set tubular construction, and described first set tubular construction limits the first vapo(u)r blasting passage, dried coal powder and main oxygen injection channel and combustion-supporting gas and the inflammable gas passage for spraying described combustion-supporting gas and described inflammable gas for spraying described dried coal powder and described main oxygen for spraying described steam.Can make thus the structure of described waste boiler type vapourizing furnace more reasonable, can further improve the transformation efficiency of charcoal in coal.
Described upper secondary nozzle is the second sleeve structure, and described the second sleeve structure limits the second vapour passage for spraying described steam, for the oxygen spray passage that sprays described oxygen with for spraying the dried coal powder injection channel of described dried coal powder.Can make thus the structure of described waste boiler type vapourizing furnace more reasonable, further increase the disturbance of the high-temperature gas in described waste boiler type vapourizing furnace, thereby can further improve the transformation efficiency of charcoal in dried coal powder.
Described upper secondary nozzle is a plurality of, and is uniformly distributed around described top main jet.Can further improve the transformation efficiency of dry powder carbon content in coal thus, further reduce the carbon residue content in lime-ash, further increase the rate of decomposition of the gas forming amount of unit mass dried coal powder, effective gas composition and steam.
Angle between the central axis of the medullary ray of each described upper secondary nozzle and described the first body of heater is the 15-30 degree.Not only the mixed effect of dried coal powder, main oxygen, combustion-supporting gas, inflammable gas, steam etc. can be further improved thus, and the space availability ratio of described combustion chamber can be improved.
Described the first body of heater comprises the first furnace shell, be located at the combustion chamber cooling jacket on the top in described the first furnace shell and be located at the first useless pot cooling room shell of the bottom in described the first furnace shell, limit described combustion chamber in the cooling jacket of described combustion chamber, be provided with the first cooling room pipe in the described first useless pot cooling room shell, limit described the first radiant cooling room in described the first cooling room pipe, limit described the first convection current cooling room between described the first cooling room pipe and the described first useless pot cooling room shell
Described combustion chamber cooling jacket, the described first useless pot cooling room shell and described the first cooling room pipe form by membrane type water wall.Can improve thus the production efficiency of described waste boiler type vapourizing furnace and to the adaptability of coal.
Be provided with the first cooling jacket consisted of membrane wall in the open top of described combustion chamber, the junction of described combustion chamber and the described first useless pot cooling room is provided with the second cooling jacket consisted of membrane wall.By described the first cooling jacket and described the second cooling jacket are set, thereby can extend the work-ing life of described combustion chamber cooling jacket, can extend the work-ing life of described the first body of heater.
Described the second body of heater comprises the second furnace shell and is located at the second useless pot cooling room shell in described the second furnace shell, be provided with the second cooling room pipe in the described second useless pot cooling room shell, limit described the second radiant cooling room in described the second cooling room pipe, limit described the second convection current cooling room between described the second cooling room pipe and the described second useless pot cooling room shell
The described second useless pot cooling room shell and described the second cooling room pipe form by membrane type water wall.Can improve the production efficiency of described waste boiler type vapourizing furnace thus.
The end of described combustion chamber cooling jacket, the first useless pot cooling room shell and the described second useless pot cooling room shell is respectively equipped with flange.Can be installed and be overhauled described combustion chamber cooling jacket, the first cooling jacket, described the second cooling jacket and described the 3rd cooling jacket more easily thus.
Be provided with the 3rd cooling jacket formed by membrane wall in the open top of the described second useless pot cooling room.By described the 3rd cooling jacket is set, thereby can extend work-ing life of the described second useless pot cooling room shell, can extend the work-ing life of described the second body of heater.
Described the first body of heater is provided with for detection of four temperature detection mouths of the temperature in described combustion chamber with for two protection gas entrances to passing into protection gas between described the first furnace shell and described combustion chamber cooling jacket.Can make thus the structure of described waste boiler type vapourizing furnace more reasonable.
Additional aspect of the present utility model and advantage part in the following description provide, and part will become obviously from the following description, or recognize by practice of the present utility model.
The accompanying drawing explanation
Above-mentioned and/or additional aspect of the present utility model and advantage are from obviously and easily understanding becoming the description of embodiment in conjunction with following accompanying drawing, wherein:
Fig. 1 is the structural representation according to the useless pot vapourizing furnace of the utility model embodiment.
Embodiment
Below describe embodiment of the present utility model in detail, the example of described embodiment is shown in the drawings, and wherein same or similar label means same or similar element or the element with identical or similar functions from start to finish.Be exemplary below by the embodiment be described with reference to the drawings, be intended to for explaining the utility model, and can not be interpreted as restriction of the present utility model.
In description of the present utility model, it will be appreciated that, term " " center ", " vertically ", " laterally ", " length ", " width ", " thickness ", " on ", D score, " front ", " afterwards ", " left side ", " right side ", " vertically ", " level ", " top ", " end " " interior ", " outward ", " clockwise ", orientation or the position relationship of indications such as " counterclockwise " are based on orientation shown in the drawings or position relationship, only the utility model and simplified characterization for convenience of description, rather than device or the element of indication or hint indication must have specific orientation, with specific orientation structure and operation, therefore can not be interpreted as restriction of the present utility model.
In addition, term " first ", " second " be only for describing purpose, and can not be interpreted as indication or hint relative importance or the implicit quantity that indicates indicated technical characterictic.Thus, one or more these features can be expressed or impliedly be comprised to the feature that is limited with " first ", " second ".In description of the present utility model, the implication of " a plurality of " is two or more, unless otherwise expressly limited specifically.
In the utility model, unless otherwise clearly defined and limited, broad understanding should be done in the terms such as term " installation ", " being connected ", " connection ", " fixing ", for example, can be to be fixedly connected with, and can be also to removably connect, or connect integratedly; Can be mechanical connection, can be also to be electrically connected to; Can be directly to be connected, also can indirectly be connected by intermediary, can be the connection of two element internals.For the ordinary skill in the art, can understand as the case may be the concrete meaning of above-mentioned term in the utility model.
In the utility model, unless otherwise clearly defined and limited, First Characteristic Second Characteristic it " on " or D score can comprise that the first and second features directly contact, also can comprise that the first and second features are not directly contacts but by the other feature contact between them.And, First Characteristic Second Characteristic " on ", " top " and " above " comprise First Characteristic directly over Second Characteristic and oblique upper, or only mean that the First Characteristic level height is higher than Second Characteristic.First Characteristic Second Characteristic " under ", " below " and " below " comprise First Characteristic under Second Characteristic and tiltedly, or only mean that the First Characteristic level height is less than Second Characteristic.
Below with reference to Fig. 1, the waste boiler type vapourizing furnace 10 according to the utility model embodiment is described.As shown in Figure 1, comprise the first body of heater 100, the second body of heater 200, top main jet 300 and upper secondary nozzle 400 according to the waste boiler type vapourizing furnace 10 of the utility model embodiment.
There is superposed combustion chamber 110 in the first body of heater 100, be positioned at the first following useless pot cooling room 120 of combustion chamber 110 and be positioned at the first following shock chamber 130 of useless pot cooling room 120, the first useless pot cooling room 120 comprises the first radiant cooling room 121 and around the first convection current cooling room 122 of the first radiant cooling room 121, the top of the first radiant cooling room 121 is communicated with 110 bottom, combustion chamber, the open bottom end of the first radiant cooling room 121, the bottom of the first convection current cooling room 122 is communicated with the bottom of the first radiant cooling room 121, the top of the first convection current cooling room 122 is provided with air outlet 1221.
There is the second useless pot cooling room 210 in the second body of heater 200, the second useless pot cooling room 210 comprises the second radiant cooling room 211 and around the second convection current cooling room 212 of the second radiant cooling room 211, the top of the second radiant cooling room 211 is communicated with air outlet 1221, the bottom of the second convection current cooling room 212 is communicated with the bottom of the second radiant cooling room 211, and the top of the second convection current cooling room 212 is provided with syngas outlet 2121.
Top main jet 300 is located at the center on the top of the first body of heater 100, top main jet 300, for 110 interior uperizes, dried coal powder, main oxygen, combustion-supporting gas and inflammable gas from 110 top, combustion chamber to combustion chamber, is provided with integrated igniting and flame detecting device in top main jet 300.Upper secondary nozzle 400 is located at the top of the first body of heater 100, for 110 interior uperizes, oxygen and dried coal powder from 110 top, combustion chamber to combustion chamber.Wherein, above-below direction is as shown in the arrow A in Fig. 1.
Useless pot cooling room according to the waste boiler type vapourizing furnace 10 of the utility model embodiment by two series connection are set (connect by the first useless pot cooling room 120 and the second useless pot cooling room 210, and the first useless pot cooling room 120 and the second useless pot cooling room 210 all comprise radiant cooling room and convection current cooling room), latent heat in high-temperature synthesis gas can be by each radiant cooling room and the heat exchange of convection current cooling room in the first useless pot cooling room 120 and the second useless pot cooling room 210, thereby can reclaim fully the latent heat of high-temperature gas, can improve heat recovery and utilization efficiency (thermo-efficiency of waste boiler type vapourizing furnace 10 can up to more than 70%).Waste boiler type vapourizing furnace 10 during for projects such as IGCC, coal high concentration COs processed, can make system thermal efficiency higher.
And, according to the waste boiler type vapourizing furnace 10 of the utility model embodiment by top main jet 300 and upper secondary nozzle 400 are set, can increase the disturbance of the high-temperature gas in waste boiler type vapourizing furnace 10, thereby what can make dried coal powder and vaporized chemical (such as main oxygen, combustion-supporting gas, inflammable gas, steam etc.) mix is more even, improved transformation efficiency, increased the dried coal powder of unit mass gas forming amount, improved the rate of decomposition of effective gas composition and steam.Wherein, in dried coal powder, the transformation efficiency of charcoal can reach more than 99.5%, can improve significantly gasification efficiency.
In addition, by top main jet 300 and upper secondary nozzle 400 are set, thereby not only can regulate more easily the load of waste boiler type vapourizing furnace 10, and can be amplified (volume that improves waste boiler type vapourizing furnace 10) to waste boiler type vapourizing furnace 10 more easily.Therefore, have that thermo-efficiency is higher, efficiency of carbon conversion is high, gasification efficiency is high, be convenient to amplify, be convenient to regulate the advantage such as load according to the waste boiler type vapourizing furnace 10 of the utility model embodiment.
As shown in Figure 1, in embodiment more of the present utility model, top main jet 300 can be the first set tubular construction, and described first set tubular construction can limit the first vapo(u)r blasting passage, dried coal powder and main oxygen injection channel and combustion-supporting gas and the inflammable gas passage for spraying described combustion-supporting gas and described inflammable gas for spraying described dried coal powder and described main oxygen for spraying described steam.Can make thus the structure of waste boiler type vapourizing furnace 10 more reasonable, can further improve the transformation efficiency of charcoal in coal.
Upper secondary nozzle 400 can be the second sleeve structure, and described the second sleeve structure can limit the second vapour passage for spraying described steam, for the oxygen spray passage that sprays described oxygen with for spraying the dried coal powder injection channel of described dried coal powder.Can make thus the structure of waste boiler type vapourizing furnace 10 more reasonable, further increase the disturbance of the high-temperature gas in waste boiler type vapourizing furnace 10, thereby can further improve the transformation efficiency of charcoal in dried coal powder.
Advantageously, upper secondary nozzle 400 can be a plurality of, and these a plurality of upper secondary nozzles 400 can be uniformly distributed around top main jet 300.Can make dried coal powder thus, main oxygen, combustion-supporting gas, inflammable gas, it is more even that steam etc. mix, improved the percussion flow in combustion chamber 110, the fine coal produced by percussion flow flow the atomization that is conducive to dried coal powder with flow field structure with the contacting of vaporized chemical, strengthened steam, the mixed effect of oxygen and dried coal powder, improved the caloic transfer rate, extended the mean residence time of dried coal powder particle, thereby further improved the transformation efficiency of charcoal in the dried coal powder, further reduced the carbon residue content in the lime-ash, further increased the gas forming amount of unit mass dried coal powder, improved the rate of decomposition of effective gas composition and steam.
In addition, by a plurality of upper secondary nozzles 400 are set, thereby can further improve the load width-adjustable ability of waste boiler type vapourizing furnace 10, greatly improve the throughput of waste boiler type vapourizing furnace 10.
Particularly, the angle between the central axis of the medullary ray of each upper secondary nozzle 400 and the first body of heater 100 can be 15 degree-30 degree.Not only the mixed effect of dried coal powder, main oxygen, combustion-supporting gas, inflammable gas, steam etc. can be further improved thus, and the space availability ratio of combustion chamber 110 can be improved.
As shown in Figure 1, in examples more of the present utility model, the first body of heater 100 can comprise the first furnace shell 140, be located at cooling jacket combustion chamber, the combustion chamber cooling jacket 150 and the first useless pot cooling room shell 160 that is located at the bottom in the first furnace shell 140 on the top in the first furnace shell 140, cooling jacket combustion chamber, combustion chamber cooling jacket 150 is interior can limit combustion chamber 110, first gives up, and pot cooling room shell 160 is interior can be provided with the first cooling room pipe 161, the first cooling room pipe 161 is interior can limit the first radiant cooling room 121, can limit the first convection current cooling room 122 between the first cooling room pipe 161 and the first useless pot cooling room shell 160.Wherein, combustion chamber cooling jacket combustion chamber cooling jacket the 150, first useless pot cooling room shell 160 and the first cooling room pipe 161 can consist of membrane type water wall.In other words, combustion chamber cooling jacket combustion chamber cooling jacket the 150, first useless pot cooling room shell 160 and the first cooling room pipe 161 can have the water wall inwall.
Thus when 10 normal operation of waste boiler type vapourizing furnace; can form the flux shielding layer on the water wall inwall of combustion chamber 110; this flux shielding layer can protect the water wall inwall of combustion chamber 110 not weather; the stress of having avoided Yin Gaowen, slag corrosion and start-stop car to produce produces and destroys and cause the waste boiler type vapourizing furnace 10 can't long-play the water wall inwall of combustion chamber 110, has improved the production efficiency of waste boiler type vapourizing furnace 10.
And, form by utilizing membrane type water wall the adaptability that cooling jacket combustion chamber, combustion chamber cooling jacket 150 can also improve 10 pairs of coals of waste boiler type vapourizing furnace greatly, and can the gasify coal of high ash melting point of waste boiler type vapourizing furnace 10.In gasification, gas is descending, lime-ash is descending along 110 center, combustion chamber.When coal fluctuates, the slag notch of 110 bottoms, combustion chamber not there will be the situation of obstruction yet, thereby has greatly improved practicality and the working efficiency of waste boiler type vapourizing furnace 10, avoids frequent the parking to clean out cinder notch.
In an example of the present utility model, as shown in Figure 1, can be provided with the first cooling jacket 171 consisted of membrane wall in the open top of combustion chamber 110, the junction of combustion chamber 110 and the first useless pot cooling room 120 can be provided with the second cooling jacket 172 consisted of membrane wall.By the first cooling jacket 171 and the second cooling jacket 172 are set, thereby can extend work-ing life of the first body of heater 100 work-ing life that can cooling jacket combustion chamber, prolonging combustion chamber cooling jacket 150.
As shown in Figure 1, in embodiment more of the present utility model, the second body of heater 200 can comprise the second furnace shell 220 and be located at the second useless pot cooling room shell 230 in the second furnace shell 220, second gives up, and pot cooling room shell 230 is interior can be provided with the second cooling room pipe 231, interior can the limiting between the second radiant cooling room 211, the second cooling room pipes 231 and the second useless pot cooling room shell 230 of the second cooling room pipe 231 can limit the second convection current cooling room 212.Wherein, the second useless pot cooling room shell 230 and the second cooling room pipe 231 can consist of membrane type water wall.In other words, the second useless pot cooling room shell 230 and the second cooling room pipe 231 can have water wall structure.
Thus when 10 normal operation of waste boiler type vapourizing furnace, the water wall inwall of the second useless pot cooling room shell 230 and the water wall of the second cooling room pipe 231 fully absorb the latent heat of high-temperature gas, reduce the air outlet temperature of vapourizing furnace, improved the thermo-efficiency of waste boiler type vapourizing furnace 10.
In an embodiment of the present utility model, as shown in Figure 1, in the open top of the second useless pot cooling room 210, can be provided with the 3rd cooling jacket 240 formed by membrane wall.By the 3rd cooling jacket 240 is set, thereby can extend work-ing life of the second useless pot cooling room shell 230, can extend the work-ing life of the second body of heater 200.
Advantageously, the end of the end of the first useless pot cooling room shell 160 and the second useless pot cooling room shell 230 can be respectively equipped with flange.Can be installed and be overhauled combustion chamber cooling jacket 150, the first cooling jacket 171, the second cooling jacket 172 and the 3rd cooling jacket 240 more easily thus.
On the first body of heater 100, can be provided with for detection of four temperature detection mouths 180 of the temperature in combustion chamber 110 with for to two that pass into protection gas between the first furnace shell 140 and cooling jacket combustion chamber, combustion chamber cooling jacket 150, protecting gas entrances 190.Can make thus the structure of waste boiler type vapourizing furnace 10 more reasonable.
In the description of this specification sheets, the description of reference term " embodiment ", " some embodiment ", " example ", " concrete example " or " some examples " etc. means to be contained at least one embodiment of the present utility model or example in conjunction with specific features, structure, material or the characteristics of this embodiment or example description.In this manual, the schematic statement of above-mentioned term not necessarily referred to identical embodiment or example.And the specific features of description, structure, material or characteristics can be with suitable mode combinations in any one or more embodiment or example.
Although the above has illustrated and has described embodiment of the present utility model, be understandable that, above-described embodiment is exemplary, can not be interpreted as restriction of the present utility model, those of ordinary skill in the art is not in the situation that break away from principle of the present utility model and aim can be changed above-described embodiment in scope of the present utility model, modification, replacement and modification.
Claims (11)
1. a waste boiler type vapourizing furnace, is characterized in that, comprising:
The first body of heater, there is superposed combustion chamber in described the first body of heater, be positioned at the useless pot cooling room in first below described combustion chamber and be positioned at the shock chamber below the described first useless pot cooling room, the described first useless pot cooling room comprises the first radiant cooling room and around the first convection current cooling room of described the first radiant cooling room, the top of described the first radiant cooling room is communicated with the bottom of described combustion chamber, the open bottom end of described the first radiant cooling room, the bottom of described the first convection current cooling room is communicated with the bottom of described the first radiant cooling room, the top of described the first convection current cooling room is provided with air outlet,
The second body of heater, there is the second useless pot cooling room in described the second body of heater, the described second useless pot cooling room comprises the second radiant cooling room and around the second convection current cooling room of described the second radiant cooling room, the top of described the second radiant cooling room is communicated with described air outlet, the bottom of described the second convection current cooling room is communicated with the bottom of described the second radiant cooling room, and the top of described the second convection current cooling room is provided with syngas outlet;
The top main jet, described top main jet is located at the center on the top of described the first body of heater, described top main jet, for uperize, dried coal powder, main oxygen, combustion-supporting gas and inflammable gas in from the top of described combustion chamber to described combustion chamber, is provided with integrated igniting and flame detecting device in the main jet of described top; The upper secondary nozzle, described upper secondary nozzle is located at the top of described the first body of heater, for the top from described combustion chamber to uperize, oxygen and dried coal powder in described combustion chamber.
2. waste boiler type vapourizing furnace according to claim 1, it is characterized in that, described top main jet is the first set tubular construction, and described first set tubular construction limits the first vapo(u)r blasting passage, dried coal powder and main oxygen injection channel and combustion-supporting gas and the inflammable gas passage for spraying described combustion-supporting gas and described inflammable gas for spraying described dried coal powder and described main oxygen for spraying described steam.
3. waste boiler type vapourizing furnace according to claim 1, it is characterized in that, described upper secondary nozzle is the second sleeve structure, and described the second sleeve structure limits the second vapour passage for spraying described steam, for the oxygen spray passage that sprays described oxygen with for spraying the dried coal powder injection channel of described dried coal powder.
4. waste boiler type vapourizing furnace according to claim 1, is characterized in that, described upper secondary nozzle is a plurality of, and be uniformly distributed around described top main jet.
5. waste boiler type vapourizing furnace according to claim 4, is characterized in that, the angle between the central axis of the medullary ray of each described upper secondary nozzle and described the first body of heater is the 15-30 degree.
6. according to the described waste boiler type vapourizing furnace of any one in claim 1-5, it is characterized in that, described the first body of heater comprises the first furnace shell, be located at the combustion chamber cooling jacket and the first useless pot cooling room shell that is located at the bottom in described the first furnace shell on the top in described the first furnace shell, limit described combustion chamber in the cooling jacket of described combustion chamber, be provided with the first cooling room pipe in the described first useless pot cooling room shell, limit described the first radiant cooling room in described the first cooling room pipe, limit described the first convection current cooling room between described the first cooling room pipe and the described first useless pot cooling room shell,
Described combustion chamber cooling jacket, the described first useless pot cooling room shell and described the first cooling room pipe form by membrane type water wall.
7. waste boiler type vapourizing furnace according to claim 6, it is characterized in that, be provided with the first cooling jacket consisted of membrane wall in the open top of described combustion chamber, the junction of described combustion chamber and the described first useless pot cooling room is provided with the second cooling jacket consisted of membrane wall.
8. waste boiler type vapourizing furnace according to claim 6, it is characterized in that, described the second body of heater comprises the second furnace shell and is located at the second useless pot cooling room shell in described the second furnace shell, be provided with the second cooling room pipe in the described second useless pot cooling room shell, limit described the second radiant cooling room in described the second cooling room pipe, limit described the second convection current cooling room between described the second cooling room pipe and the described second useless pot cooling room shell
The described second useless pot cooling room shell and described the second cooling room pipe form by membrane type water wall.
9. waste boiler type vapourizing furnace according to claim 8, is characterized in that, the end of described combustion chamber cooling jacket, the first useless pot cooling room shell and the described second useless pot cooling room shell is respectively equipped with flange.
10. waste boiler type vapourizing furnace according to claim 8, is characterized in that, in the open top of the described second useless pot cooling room, is provided with the 3rd cooling jacket consisted of membrane wall.
11. waste boiler type vapourizing furnace according to claim 6; it is characterized in that, described the first body of heater is provided with for detection of four temperature detection mouths of the temperature in described combustion chamber with for two protection gas entrances to passing into protection gas between described the first furnace shell and described combustion chamber cooling jacket.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013203696631U CN203333601U (en) | 2013-06-25 | 2013-06-25 | Waste-boiler-type gasification furnace |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013203696631U CN203333601U (en) | 2013-06-25 | 2013-06-25 | Waste-boiler-type gasification furnace |
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| CN203333601U true CN203333601U (en) | 2013-12-11 |
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| Application Number | Title | Priority Date | Filing Date |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103387851A (en) * | 2013-06-25 | 2013-11-13 | 上海鑫兴化工科技有限公司 | Waste heat boiler-type gasifier |
| CN103820169A (en) * | 2014-03-11 | 2014-05-28 | 上海锅炉厂有限公司 | Combined cooling and purifying device and method for high-temperature raw gas |
-
2013
- 2013-06-25 CN CN2013203696631U patent/CN203333601U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103387851A (en) * | 2013-06-25 | 2013-11-13 | 上海鑫兴化工科技有限公司 | Waste heat boiler-type gasifier |
| CN103387851B (en) * | 2013-06-25 | 2015-12-23 | 上海尧兴投资管理有限公司 | Waste heat boiler-type gasifier |
| CN103820169A (en) * | 2014-03-11 | 2014-05-28 | 上海锅炉厂有限公司 | Combined cooling and purifying device and method for high-temperature raw gas |
| CN103820169B (en) * | 2014-03-11 | 2015-08-19 | 上海锅炉厂有限公司 | A kind of combined type height temperature rough gas cooling purifying device and method |
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Owner name: SHANGHAI YAOXING INVESTMENT MANAGEMENT CO., LTD. Free format text: FORMER OWNER: SHANGHAI XINXING CHEMICAL TECHNOLOGY CO., LTD. Effective date: 20150716 |
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