WO2013107006A1 - Garbage pyrolyzing and gasifying furnace - Google Patents
Garbage pyrolyzing and gasifying furnace Download PDFInfo
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- WO2013107006A1 WO2013107006A1 PCT/CN2012/070531 CN2012070531W WO2013107006A1 WO 2013107006 A1 WO2013107006 A1 WO 2013107006A1 CN 2012070531 W CN2012070531 W CN 2012070531W WO 2013107006 A1 WO2013107006 A1 WO 2013107006A1
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- flue gas
- combustion chamber
- gas combustion
- main combustion
- passage
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
- F23G5/14—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
- F23G5/16—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/033—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment comminuting or crushing
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/24—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having a vertical, substantially cylindrical, combustion chamber
- F23G5/26—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having a vertical, substantially cylindrical, combustion chamber having rotating bottom
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/32—Incineration of waste; Incinerator constructions; Details, accessories or control therefor the waste being subjected to a whirling movement, e.g. cyclonic incinerators
Definitions
- the invention relates to a garbage waste treatment device, in particular to a pyrolysis gasification furnace for urban domestic garbage, medical hazardous waste, dried sludge, industrial solid waste and the like. Background technique
- the main treatment methods include incineration, composting and sanitary landfill. Among these three methods, incineration is the best way to achieve harmlessness, reduction and recycling of waste.
- the waste incineration treatment system is further divided into a direct incineration system and a pyrolysis incineration system according to the combustion mode. Due to the high pyrolysis temperature, the pyrolysis incineration system treats the pollutants in the flue gas after the waste combustion more fully and is more environmentally friendly.
- the inventors have disclosed a garbage pyrolysis gasification furnace with a vertical sleeve structure.
- the main combustion chamber and the second combustion chamber adopt a coaxial sleeve design, and fully utilize the convection and conduction of thermal energy. Radiation to increase the temperature of the second combustion chamber, without the need to add auxiliary fuel to assist combustion, that is, the temperature of the second combustion chamber can reach the standard, and the residence time of the flue gas is above 9O0 °C for more than 2 seconds, which greatly reduces the running cost.
- the present invention provides a garbage pyrolysis gasification furnace which can improve the utilization efficiency of the combustion heat energy of the main combustion chamber of the pyrolysis gasification furnace and further ensure the combustion of the flue gas more fully.
- the garbage pyrolysis gasification furnace comprises a cylindrical main combustion chamber, a top of the main combustion chamber is provided with a feed port for discharging waste waste, and a bottom of the main combustion chamber is provided with a grate for removing waste residue and feeding air.
- the main combustion chamber has a furnace wall for heat storage and heat transfer
- the garbage pyrolysis gasification furnace further comprises a flue gas combustion passage disposed along the circumference of the main combustion chamber, and a part of the inner surface of the flue gas combustion chamber is outside the furnace wall of the main combustion chamber Surface composition, the thermal energy of the main combustion chamber and the flue gas combustion chamber can be mutually transmitted through the main combustion chamber wall, the flue gas combustion chamber
- the utility model comprises a smoke inlet, a flue gas combustion passage and a smoke exhaust port, wherein the smoke inlet is arranged at an upper part of the main combustion chamber wall, and the flue gas combustion passage comprises a first part of the flue gas combustion passage and a second part of the flue gas combustion passage, the main combustion chamber
- the formed flue gas passes through the first portion of the flue gas combustion passage and the second portion of the flue gas combustion passage through the inlet, and is discharged from the exhaust port of the flue gas combustion chamber, and the cross-sectional area of the first portion of the
- the main combustion chamber has a furnace wall for heat storage and heat transfer, and a part of the inner surface of the combustion chamber of the flue gas is composed of the outer surface of the furnace wall of the main combustion chamber, the main combustion chamber and the smoke
- the heat energy between the gas combustion passages can conduct to each other, and at the same time, the two combustion chambers function as heat radiation, thereby ensuring that the main combustion chamber and the flue gas combustion passage can maintain sufficient combustion temperature without adding any auxiliary fuel;
- the cross-sectional area of the first portion of the flue gas combustion passage is smaller than the cross-sectional area of the second portion of the flue gas combustion passage, the flow rate of the flue gas formed by the main combustion chamber is relatively slow, when the flue gas flows past the first portion of the flue gas combustion passage, As the cross-sectional area decreases, the flue gas flow rate becomes faster, and when it flows through the second portion of the flue gas combustion passage, the flue gas flow rate becomes faster and
- Figure 1 is a schematic illustration of a partially sectioned refuse pyrolysis gasification system employing an embodiment of a waste pyrolysis gasifier of the present invention.
- Figure 2 is a cross-sectional view of an embodiment of a waste pyrolysis gasification furnace 200.
- Figure 3 is a longitudinal cross-sectional view of the embodiment of Figure 2 taken along line AB of Figure 2.
- Fig. 4 shows a schematic view of a flue gas combustion passage spirally disposed along the outer circumference of the main combustion chamber.
- Fig. 5 shows a cross-sectional view of another embodiment of the pyrolysis gasification furnace of the present invention.
- Figure 6 is a cross-sectional view showing still another embodiment of the pyrolysis gasification furnace of the present invention. detailed description
- FIG. 1 is a schematic illustration of a partially sectioned refuse pyrolysis gasification system employing an embodiment of a waste pyrolysis gasifier of the present invention.
- the waste pyrolysis gasification system 10 includes a blanking device 100, a garbage pyrolysis gasification furnace 200, a rotary grate 300, a slagging device 400, a drive and control device 500, and a blower device (not shown).
- the unloading device 100 feeds the garbage waste into the interior of the garbage pyrolysis gasification furnace 200 through the feed port 201 provided above the garbage pyrolysis gasification furnace 200.
- the rotary grate 300 is disposed at a lower portion of the waste pyrolysis gasification furnace 200 for discharging the slag generated after the pyrolysis of the waste into the slag removal device 400, and the slag removal device 400 discharges the slag to the waste pyrolysis gasification furnace 200 for subsequent Processing program.
- a blower (not shown) is used to deliver external air to the waste pyrolysis gasifier 200 to provide sufficient oxygen for combustion use.
- the waste pyrolysis gasification system 10 further includes a drive and control device 500 for driving and controlling the various components of the waste pyrolysis gasification system. The present invention is directed to the modification of the waste pyrolysis gasification furnace 200.
- FIG. 1 only exemplarily shows the main structure of the garbage pyrolysis gasification system, and the details thereof are not limited thereto.
- Figure 2 is a cross-sectional view of an embodiment of a waste pyrolysis gasification furnace 200.
- Figure 3 is a longitudinal cross-sectional view of the embodiment of Figure 2 taken along line AB of Figure 2.
- the waste pyrolysis gasification furnace 200 includes a cylindrical main combustion chamber 210 and a flue gas combustion chamber 220 disposed along the circumference of the main combustion chamber.
- the main combustion chamber 210 is used for pyrolysis gasification of various solid waste wastes.
- the flue gas combustion chamber 220 is used to further decompose and decompose the flue gas containing various vaporized wastes from the main combustion chamber.
- the flue gas removed from the flue gas combustor 220 will be used for subsequent processing, including thermal power generation, flue gas purification, and the like.
- the main burner top 210 is provided with a feed port 201 for dispensing waste.
- a rotary grate 300 for removing waste and feeding air is installed at the bottom of the main combustion chamber 210.
- the furnace wall 205 of the main combustion chamber is composed of a material having a good heat storage and heat transfer property, and can accumulate and conduct heat generated when the waste waste is burned in the main combustion chamber.
- the furnace wall 205 is constructed of high temperature refractory bricks, such as high alumina bricks.
- the flue gas combustion chamber 220 is disposed around the cylindrical main combustion chamber 210 such that a portion of the inner surface of the flue gas combustion chamber 220 is formed by the outer surface of the furnace wall 205 of the main combustion chamber.
- the furnace wall 205 capable of regenerative heat transfer can accumulate and transfer the heat generated by the pyrolysis of the main combustion chamber to the flue gas combustion chamber 220, and can also generate high-temperature energy generated by the combustion of the flue gas in the flue gas combustion chamber 220. Accumulated and conducted back to the main combustion chamber 210 to provide thermal energy for subsequent waste disposal.
- the furnace wall 205 effectively communicates the two thermodynamic spaces of the main combustion chamber 210 and the flue gas combustion chamber 220 to maximize the utilization of energy generated in the waste waste treatment.
- Use the pyrolysis gasifier designed as above in the garbage after the initial oven It is no longer necessary to add any auxiliary fuel in the process, and rely on the energy generated by the pyrolysis of the waste waste to increase the stable energy source for the subsequently treated garbage.
- the flue gas combustion chamber 220 includes a smoke inlet 221, a flue gas combustion passage 230, and a smoke exhaust port 222.
- the outer wall of the flue gas combustion chamber 220 forms a cylinder coaxial with the main combustion chamber 210.
- An axially extending partition 235 and a partition 236 are disposed between the main combustion chamber 210 and the flue gas combustion chamber 220 to form a sector-shaped compartment as shown in FIG. 2 to form a first portion 231 of the flue gas combustion passage 230 and The second part 232.
- the partition 235 and the partition 236 are closed to the top plate 250 of the pyrolysis gasification furnace and are not closed from the bottom plate 260, so that the first portion 231 and the lower portion of the second portion 232 are in communication.
- the smoke inlet 221 is disposed at an upper portion of the main combustion chamber wall 205 and communicates with the first portion 231.
- the smoke exhaust port 222 of the flue gas combustion chamber may be disposed flush with or above the smoke inlet, but in communication with the second portion 232. In the illustrated embodiment, the flue gas combustion chamber The smoke exhaust port 222 is disposed at the top of the flue gas combustion chamber 220.
- the first portion 231 of the flue gas combustion passage extends downwardly from the inlet 221 to the lower portion of the compartment, and the second portion 232 of the flue gas passage extends upwardly from the lower portion of the compartment to the vent 222.
- the flue gas formed by the main combustion chamber passes through the flue gas combustion passage first portion 231 and the flue gas combustion passage second portion 232 through the flue gas inlet 221, and is discharged from the flue gas exhaust port 222 of the flue gas combustion passage.
- the cross-sectional area of the first portion 231 of the flue gas combustion passage is less than the cross-sectional area 232 of the second portion of the flue gas combustion passage. Since the cross-sectional area of the first portion of the flue gas combustion passage is smaller than the cross-sectional area of the second portion of the flue gas combustion passage, the flow rate of the flue gas formed by the main combustion chamber is slower, when the flue gas flows past the first portion of the flue gas combustion passage, due to the cross section As the area decreases, the flue gas flow rate becomes faster, and when it flows through the second part of the flue gas combustion passage, the flue gas flow rate becomes faster and slower due to the increased cross-sectional area. In this way, the change of the flue gas flow rate through the three states of slow-fast-slow can ensure that the flue gas is burned more fully, so that the harmful substances in the flue gas are more thoroughly removed.
- the outer wall 237 of the flue gas combustion chamber completely encloses the main combustion chamber 210, and the furnace wall 205 of the main combustion chamber is not exposed to the air.
- the outer wall 237 of the flue gas combustion chamber includes an insulating material to prevent heat loss.
- the flue gas combustion passage 230 includes a descending first portion 231 and an upward second portion 232. Its total length is approximately equal to twice the vertical height of the main combustion chamber. However, as long as the path length of the flue gas flow between the inlet to the exhaust port is sufficiently long, such as at least greater than the vertical height of the main combustion chamber, the arrangement of the flue gas combustion passage is not limited to a straight line. 4 shows a flue gas combustion passage spirally disposed along the outer circumference of the main combustion chamber 210, wherein the smaller the helix angle, the longer the length of the flue gas combustion passage, and the more the path of the flue gas flow Long.
- the flue gas combustion chamber may include a plurality of flue gas combustion passages.
- Figure 5 is a cross-sectional view showing another embodiment of the pyrolysis gasification furnace of the present invention, wherein four (and of course more) are disposed between the flue gas combustion outdoor wall and the main combustion chamber wall. An axially extending partition, thereby forming four compartments having a sectoral shape (two large and two small in area), wherein the areas of the two sectors are equal.
- each compartment is connected, and each compartment is provided with a corresponding inlet or exhaust vent, thereby forming two first portions of the flue gas combustion passage extending from the inlet to the lower portion of the compartment. And two portions of the flue gas combustion passage having a larger cross-sectional area extending from the lower portion of the compartment to the exhaust vent, forming two flue gas combustion passages.
- the outer wall of the flue gas combustion chamber may be cylindrical, it may have other shapes, as shown in Fig. 6, in the same manner as the other parts of the embodiment of Fig. 5, in order to ensure the cross section of the second portion of the flue gas combustion passage.
- the area is large enough to increase the diameter of the outer sector of the sector, so that the outer wall of the flue gas combustion chamber has lugs instead of a uniform cylinder.
- the flue gas combustion chamber completely surrounds the main combustion chamber so that the furnace wall of the main combustion chamber is not exposed to the air, thereby
- the heat storage and heat transfer of the furnace wall of the main combustion chamber can be fully utilized, as shown in the various embodiments of the drawings.
- a plurality of air blowing holes may be provided in the flue gas combustion passage, such as the air blowing holes 237, 238 shown in Fig. 2.
- the air vents may include a plurality of air streams that are arranged to be blown in a direction perpendicular to the path of the smoke flow to form a uniform hook.
- the flue gas flows through the air blowing holes, it mixes with the fresh air flowing in through the air blowing holes to further fully burn, so that the harmful substances in the flue gas are completely decomposed.
- the number and specific position of the above air blowing holes are not limited to those shown in the drawings, and those skilled in the art can calculate the specific conditions such as the amount of waste disposal, the size of the pyrolysis gasifier, and the like.
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- General Engineering & Computer Science (AREA)
- Gasification And Melting Of Waste (AREA)
- Incineration Of Waste (AREA)
Description
垃圾热解气化炉 技术领域 Waste pyrolysis gasification furnace
本发明涉及一种垃圾废物的处理装置, 特别是一种用于城市生活垃圾、 医疗危险废物、 干化后的污泥、 工业固体废物等的热解气化炉。 背景技术 The invention relates to a garbage waste treatment device, in particular to a pyrolysis gasification furnace for urban domestic garbage, medical hazardous waste, dried sludge, industrial solid waste and the like. Background technique
随着社会的发展, 人们的环保意识日益增强。 各国的科学家都在致力于 环保节能技术的研发。 对于垃圾废物的处理和再利用, 也提出了各种各样的 解决方案。 主要的处理方式包括焚烧、 堆肥和卫生填埋。 在这三种方式中, 焚烧法是垃圾无害化、 减量化和资源化的最好途径。 垃圾焚烧处理系统按照 燃烧方式又分为直接焚烧系统和热解焚烧系统。 热解焚烧系统由于热解温度 高, 对垃圾燃烧后的烟气中的污染物处理更充分, 更符合环保的要求。 With the development of society, people's awareness of environmental protection is increasing. Scientists from all over the world are working on the development of environmentally friendly and energy-saving technologies. Various solutions have also been proposed for the disposal and reuse of waste. The main treatment methods include incineration, composting and sanitary landfill. Among these three methods, incineration is the best way to achieve harmlessness, reduction and recycling of waste. The waste incineration treatment system is further divided into a direct incineration system and a pyrolysis incineration system according to the combustion mode. Due to the high pyrolysis temperature, the pyrolysis incineration system treats the pollutants in the flue gas after the waste combustion more fully and is more environmentally friendly.
本发明人于 2005年 7月 1日提交了发明名称为 "医疗垃圾焚烧炉"的中国 发明专利申请, 该申请于 2008年 4月 9日授权公告。 在该专利中, 本发明人公 开了一种立式套筒结构的垃圾热解气化炉, 主燃室和二燃室采用同轴套筒式 设计, 并充分利用了热能的对流、 传导和辐射来提高二燃室的温度, 无须添 加辅助燃料助燃, 即能使二燃室温度达标、 烟气停留时间在 9O0 °C以上超过 2 秒以上, 大大减少了运行成本。 The inventor filed a Chinese invention patent application entitled "Medical Waste Incinerator" on July 1, 2005, which was issued on April 9, 2008. In this patent, the inventors have disclosed a garbage pyrolysis gasification furnace with a vertical sleeve structure. The main combustion chamber and the second combustion chamber adopt a coaxial sleeve design, and fully utilize the convection and conduction of thermal energy. Radiation to increase the temperature of the second combustion chamber, without the need to add auxiliary fuel to assist combustion, that is, the temperature of the second combustion chamber can reach the standard, and the residence time of the flue gas is above 9O0 °C for more than 2 seconds, which greatly reduces the running cost.
在上述发明实施的过程中, 本发明人一直在探索如何进一步提高主燃室 燃烧热能的利用效率, 并且进一步保证烟气燃烧更充分而达到完全燃烧的状 态, 以便更彻底地去处烟气中的有害物质。 发明内容 In the course of the implementation of the above invention, the inventors have been exploring how to further improve the utilization efficiency of the combustion heat energy of the main combustion chamber, and further ensure that the combustion of the flue gas is more complete and reaches a state of complete combustion, so as to more thoroughly go to the flue gas. Harmful Substance. Summary of the invention
为了解决上述问题, 本发明提供了一种垃圾热解气化炉, 可以提高热解 气化炉主燃室燃烧热能的利用效率, 并且进一步保证烟气燃烧更充分。 In order to solve the above problems, the present invention provides a garbage pyrolysis gasification furnace which can improve the utilization efficiency of the combustion heat energy of the main combustion chamber of the pyrolysis gasification furnace and further ensure the combustion of the flue gas more fully.
根据本发明的垃圾热解气化炉, 包括圓筒状主燃室, 主燃室顶部设有用 于投放垃圾废物的进料口, 主燃室底部安装有用于排除废渣和送入空气的炉 排, 主燃室具有蓄热传热的炉壁, 垃圾热解气化炉还包括沿主燃室外周设置 的烟气燃烧通道, 烟气燃烧室的内表面的一部分由主燃室的炉壁外表面构 成, 主燃室与烟气燃烧室的热能能够通过主燃室炉壁相互传导, 烟气燃烧室 包括进烟口、 烟气燃烧通道和排烟口, 进烟口设置在主燃室炉壁的上部, 烟 气燃烧通道包括烟气燃烧通道第一部分和烟气燃烧通道第二部分, 主燃室形 成的烟气通过进烟口依次经过烟气燃烧通道第一部分和烟气燃烧通道第二 部分, 而由烟气燃烧室的排烟口排出, 烟气燃烧通道第一部分的横截面积小 于烟气燃烧通道第二部分的截面积。 The garbage pyrolysis gasification furnace according to the present invention comprises a cylindrical main combustion chamber, a top of the main combustion chamber is provided with a feed port for discharging waste waste, and a bottom of the main combustion chamber is provided with a grate for removing waste residue and feeding air. The main combustion chamber has a furnace wall for heat storage and heat transfer, and the garbage pyrolysis gasification furnace further comprises a flue gas combustion passage disposed along the circumference of the main combustion chamber, and a part of the inner surface of the flue gas combustion chamber is outside the furnace wall of the main combustion chamber Surface composition, the thermal energy of the main combustion chamber and the flue gas combustion chamber can be mutually transmitted through the main combustion chamber wall, the flue gas combustion chamber The utility model comprises a smoke inlet, a flue gas combustion passage and a smoke exhaust port, wherein the smoke inlet is arranged at an upper part of the main combustion chamber wall, and the flue gas combustion passage comprises a first part of the flue gas combustion passage and a second part of the flue gas combustion passage, the main combustion chamber The formed flue gas passes through the first portion of the flue gas combustion passage and the second portion of the flue gas combustion passage through the inlet, and is discharged from the exhaust port of the flue gas combustion chamber, and the cross-sectional area of the first portion of the flue gas combustion passage is smaller than the flue gas. The cross-sectional area of the second portion of the combustion passage.
本发明的垃圾热解气化炉, 由于主燃室具有蓄热传热的炉壁, 而烟气燃 烧通道的内表面的一部分由主燃室的炉壁外表面构成, 则主燃室与烟气燃烧 通道之间的热能可以相互传导, 同时对两个燃烧室起着热辐射的功能, 从而 保证主燃室和烟气燃烧通道都可以保持足够的燃烧温度, 而无需再添加任何 辅助燃料; 同时, 又由于烟气燃烧通道第一部分的横截面积小于烟气燃烧通 道第二部分的截面积, 主燃室形成的烟气流速较慢, 当烟气流过烟气燃烧通 道第一部分时, 由于横截面积减小, 烟气流速变快, 再流过烟气燃烧通道第 二部分时, 由于横截面积增大, 烟气流速变快又变慢。 这样, 烟气流速经过 慢 -快-慢三种状态的变化, 可以保证烟气燃烧得更充分, 从而更彻底地去处 烟气中的有害物质。 附图说明 In the garbage pyrolysis gasification furnace of the present invention, since the main combustion chamber has a furnace wall for heat storage and heat transfer, and a part of the inner surface of the combustion chamber of the flue gas is composed of the outer surface of the furnace wall of the main combustion chamber, the main combustion chamber and the smoke The heat energy between the gas combustion passages can conduct to each other, and at the same time, the two combustion chambers function as heat radiation, thereby ensuring that the main combustion chamber and the flue gas combustion passage can maintain sufficient combustion temperature without adding any auxiliary fuel; At the same time, since the cross-sectional area of the first portion of the flue gas combustion passage is smaller than the cross-sectional area of the second portion of the flue gas combustion passage, the flow rate of the flue gas formed by the main combustion chamber is relatively slow, when the flue gas flows past the first portion of the flue gas combustion passage, As the cross-sectional area decreases, the flue gas flow rate becomes faster, and when it flows through the second portion of the flue gas combustion passage, the flue gas flow rate becomes faster and slower due to the increased cross-sectional area. In this way, the flow rate of the flue gas changes through three states: slow-fast-slow, which ensures that the flue gas is burned more fully, so that the harmful substances in the flue gas are more thoroughly removed. DRAWINGS
为了更清楚地说明本发明实施例的技术方案, 下面将对实施例或现有技 术描述中所需要使用的附图作筒单地介绍, 显而易见地, 下面描述中的附图 仅仅是本发明的一些实施例, 对于本领域普通技术人员来讲, 在不付出创造 性劳动的前提下, 还可以根据这些附图获得其他的附图。 In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings to be used in the embodiments or the description of the prior art will be briefly described below. Obviously, the drawings in the following description are only the present invention. For some embodiments, other drawings may be obtained from those of ordinary skill in the art without departing from the drawings.
图 1为采用本发明的垃圾热解气化炉一个实施例的局部剖开的垃圾热解 气化系统的示意图。 BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a schematic illustration of a partially sectioned refuse pyrolysis gasification system employing an embodiment of a waste pyrolysis gasifier of the present invention.
图 2为垃圾热解气化炉 200—个实施例的横剖截面图。 Figure 2 is a cross-sectional view of an embodiment of a waste pyrolysis gasification furnace 200.
图 3为沿图 2中 AB线截取的图 2实施例的纵向剖视图。 Figure 3 is a longitudinal cross-sectional view of the embodiment of Figure 2 taken along line AB of Figure 2.
图 4示出了沿主燃室的外周螺旋形设置的烟气燃烧通道的示意图。 图 5示出了本发明热解气化炉的另一个实施例的横截面图。 Fig. 4 shows a schematic view of a flue gas combustion passage spirally disposed along the outer circumference of the main combustion chamber. Fig. 5 shows a cross-sectional view of another embodiment of the pyrolysis gasification furnace of the present invention.
图 6示出本发明热解气化炉的又一个实施例的横截面图。 具体实施方式 Figure 6 is a cross-sectional view showing still another embodiment of the pyrolysis gasification furnace of the present invention. detailed description
下面参照附 图 1 为采用本发明的垃圾热解气化炉一个实施例的局部剖开的垃圾热解 气化系统的示意图。垃圾热解气化系统 10包括下料装置 100、垃圾热解气化 炉 200、 旋转炉排 300、 排渣装置 400、 驱动及控制装置 500及送风装置(未 示出)。 下料装置 100将垃圾废物通过设置在垃圾热解气化炉 200上方的进 料口 201送入垃圾热解气化炉 200内部。旋转炉排 300设置在垃圾热解气化 炉 200的下部, 用于将垃圾热解后产生的炉渣排入除渣装置 400, 除渣装置 400将炉渣排出垃圾热解气化炉 200而进行后续处理程序。 送风装置(未示 出 )用于向垃圾热解气化炉 200输送外部空气, 以便提供足够的氧气供燃烧 使用。 另外, 该垃圾热解气化系统 10还包括驱动及控制装置 500, 用于驱动 和控制垃圾热解气化系统的上述各组成部分。本发明致力于对垃圾热解气化 炉 200的改造, 下料装置 100、 旋转炉排 300、 排渣装置 400、 驱动及控制装 置 500、 送风装置等可以采用本发明各种现有的结构。 另外, 图 1只示例性 显示了垃圾热解气化系统的主要结构, 其细节部分并不限于此。 Reference below BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a schematic illustration of a partially sectioned refuse pyrolysis gasification system employing an embodiment of a waste pyrolysis gasifier of the present invention. The waste pyrolysis gasification system 10 includes a blanking device 100, a garbage pyrolysis gasification furnace 200, a rotary grate 300, a slagging device 400, a drive and control device 500, and a blower device (not shown). The unloading device 100 feeds the garbage waste into the interior of the garbage pyrolysis gasification furnace 200 through the feed port 201 provided above the garbage pyrolysis gasification furnace 200. The rotary grate 300 is disposed at a lower portion of the waste pyrolysis gasification furnace 200 for discharging the slag generated after the pyrolysis of the waste into the slag removal device 400, and the slag removal device 400 discharges the slag to the waste pyrolysis gasification furnace 200 for subsequent Processing program. A blower (not shown) is used to deliver external air to the waste pyrolysis gasifier 200 to provide sufficient oxygen for combustion use. Additionally, the waste pyrolysis gasification system 10 further includes a drive and control device 500 for driving and controlling the various components of the waste pyrolysis gasification system. The present invention is directed to the modification of the waste pyrolysis gasification furnace 200. The blanking device 100, the rotary grate 300, the slagging device 400, the driving and control device 500, the air blowing device, and the like can employ various existing structures of the present invention. . In addition, FIG. 1 only exemplarily shows the main structure of the garbage pyrolysis gasification system, and the details thereof are not limited thereto.
图 2为垃圾热解气化炉 200—个实施例的横剖截面图。 图 3为沿图 2中 AB线截取的图 2实施例的纵向剖视图。在该实施例中,垃圾热解气化炉 200 包括圓筒状主燃室 210和沿主燃室外周设置的烟气燃烧室 220。 Figure 2 is a cross-sectional view of an embodiment of a waste pyrolysis gasification furnace 200. Figure 3 is a longitudinal cross-sectional view of the embodiment of Figure 2 taken along line AB of Figure 2. In this embodiment, the waste pyrolysis gasification furnace 200 includes a cylindrical main combustion chamber 210 and a flue gas combustion chamber 220 disposed along the circumference of the main combustion chamber.
主燃室 210用于各种固体的垃圾废物热解气化。 烟气燃烧室 220用于使 来自主燃室的含有各种气化后的废物的烟气进一步燃烧分解。从烟气燃烧室 220排除的烟气将用于后续的处理, 包括热能发电、 烟气净化等装置。 The main combustion chamber 210 is used for pyrolysis gasification of various solid waste wastes. The flue gas combustion chamber 220 is used to further decompose and decompose the flue gas containing various vaporized wastes from the main combustion chamber. The flue gas removed from the flue gas combustor 220 will be used for subsequent processing, including thermal power generation, flue gas purification, and the like.
主燃室顶部 210设有用于投放垃圾废物的进料口 201。主燃室 210底部安 装有用于排除废渣和送入空气的旋转炉排 300。 主燃室的炉壁 205由蓄热传 热性能好的材料构成, 可以积蓄和传导垃圾废物在主燃室燃烧时产生的热 量。 在一个优选的方案中, 炉壁 205由高温耐火砖砌筑而成, 比如采用高铝 砖。 The main burner top 210 is provided with a feed port 201 for dispensing waste. A rotary grate 300 for removing waste and feeding air is installed at the bottom of the main combustion chamber 210. The furnace wall 205 of the main combustion chamber is composed of a material having a good heat storage and heat transfer property, and can accumulate and conduct heat generated when the waste waste is burned in the main combustion chamber. In a preferred embodiment, the furnace wall 205 is constructed of high temperature refractory bricks, such as high alumina bricks.
烟气燃烧室 220围绕圓筒状主燃室 210设置,从而使得的烟气燃烧室 220 内表面的一部分由主燃室的炉壁 205外表面构成的。 这样, 可以蓄热传热的 炉壁 205 既可以将主燃室垃圾热解产生的热量积蓄并传导到烟气燃烧室 220, 也可以将烟气在烟气燃烧室 220 中燃烧产生的高温能量积蓄并传导回 主燃室 210, 从而为后续垃圾废物的处理提供热能。 由此, 炉壁 205有效地 连通了主燃室 210和烟气燃烧室 220这两个热力学空间, 最大化地利用垃圾 废物处理中产生的能量。采用如上设计的热解气化炉在初始烘炉后的垃圾处 理过程中不再需要添加任何辅助燃料, 依靠垃圾废物自身热解产生的能量, 即可为后续处理的垃圾提高稳定的能量来源。 The flue gas combustion chamber 220 is disposed around the cylindrical main combustion chamber 210 such that a portion of the inner surface of the flue gas combustion chamber 220 is formed by the outer surface of the furnace wall 205 of the main combustion chamber. In this way, the furnace wall 205 capable of regenerative heat transfer can accumulate and transfer the heat generated by the pyrolysis of the main combustion chamber to the flue gas combustion chamber 220, and can also generate high-temperature energy generated by the combustion of the flue gas in the flue gas combustion chamber 220. Accumulated and conducted back to the main combustion chamber 210 to provide thermal energy for subsequent waste disposal. Thus, the furnace wall 205 effectively communicates the two thermodynamic spaces of the main combustion chamber 210 and the flue gas combustion chamber 220 to maximize the utilization of energy generated in the waste waste treatment. Use the pyrolysis gasifier designed as above in the garbage after the initial oven It is no longer necessary to add any auxiliary fuel in the process, and rely on the energy generated by the pyrolysis of the waste waste to increase the stable energy source for the subsequently treated garbage.
烟气燃烧室 220包括进烟口 221、 烟气燃烧通道 230和排烟口 222。 在本 实施例中, 烟气燃烧室 220的外壁形成与主燃室 210同轴的圓筒。 在主燃室 210和烟气燃烧室 220之间设置沿轴向延伸的隔板 235和隔板 236, 从而形 成而图 2所示的扇形隔室而形成烟气燃烧通道 230的第一部分 231和第二部 分 232。 隔板 235和隔板 236与热解气化炉的顶板 250封闭而与底板 260之 间不封闭, 从而第一部分 231和第二部分 232下部连通。 进烟口 221设置在 主燃室炉壁 205的上部, 与第一部分 231连通。 烟气燃烧室的排烟口 222可 以设在与所述进烟口平齐或位于所述进烟口之上, 但与第二部分 232连通, 在图示实施例中, 烟气燃烧室的排烟口 222设置在烟气燃烧室 220顶部。 由 此, 烟气燃烧通道第一部分 231从进烟口 221向下延伸到隔室下部, 烟气燃 烧通道第二部分 232从隔室下部向上延伸到排烟口 222。 主燃室形成的烟气 通过进烟口 221依次经过烟气燃烧通道第一部分 231和烟气燃烧通道第二部 分 232, 而由所述烟气燃烧通道的排烟口 222排出。 The flue gas combustion chamber 220 includes a smoke inlet 221, a flue gas combustion passage 230, and a smoke exhaust port 222. In the present embodiment, the outer wall of the flue gas combustion chamber 220 forms a cylinder coaxial with the main combustion chamber 210. An axially extending partition 235 and a partition 236 are disposed between the main combustion chamber 210 and the flue gas combustion chamber 220 to form a sector-shaped compartment as shown in FIG. 2 to form a first portion 231 of the flue gas combustion passage 230 and The second part 232. The partition 235 and the partition 236 are closed to the top plate 250 of the pyrolysis gasification furnace and are not closed from the bottom plate 260, so that the first portion 231 and the lower portion of the second portion 232 are in communication. The smoke inlet 221 is disposed at an upper portion of the main combustion chamber wall 205 and communicates with the first portion 231. The smoke exhaust port 222 of the flue gas combustion chamber may be disposed flush with or above the smoke inlet, but in communication with the second portion 232. In the illustrated embodiment, the flue gas combustion chamber The smoke exhaust port 222 is disposed at the top of the flue gas combustion chamber 220. Accordingly, the first portion 231 of the flue gas combustion passage extends downwardly from the inlet 221 to the lower portion of the compartment, and the second portion 232 of the flue gas passage extends upwardly from the lower portion of the compartment to the vent 222. The flue gas formed by the main combustion chamber passes through the flue gas combustion passage first portion 231 and the flue gas combustion passage second portion 232 through the flue gas inlet 221, and is discharged from the flue gas exhaust port 222 of the flue gas combustion passage.
如图所示, 烟气燃烧通道第一部分 231 的横截面积小于烟气燃烧通道第 二部分的截面积 232。 由于烟气燃烧通道第一部分的横截面积小于烟气燃烧 通道第二部分的截面积, 主燃室形成的烟气流速较慢, 当烟气流过烟气燃烧 通道第一部分时, 由于横截面积减小, 烟气流速变快, 再流过烟气燃烧通道 第二部分时, 由于横截面积增大, 烟气流速变快又变慢。 这样, 烟气流速经 过慢 -快-慢三种状态的变化, 可以保证烟气燃烧得更充分, 从而更彻底地去 处烟气中的有害物质。 As shown, the cross-sectional area of the first portion 231 of the flue gas combustion passage is less than the cross-sectional area 232 of the second portion of the flue gas combustion passage. Since the cross-sectional area of the first portion of the flue gas combustion passage is smaller than the cross-sectional area of the second portion of the flue gas combustion passage, the flow rate of the flue gas formed by the main combustion chamber is slower, when the flue gas flows past the first portion of the flue gas combustion passage, due to the cross section As the area decreases, the flue gas flow rate becomes faster, and when it flows through the second part of the flue gas combustion passage, the flue gas flow rate becomes faster and slower due to the increased cross-sectional area. In this way, the change of the flue gas flow rate through the three states of slow-fast-slow can ensure that the flue gas is burned more fully, so that the harmful substances in the flue gas are more thoroughly removed.
烟气燃烧室的外壁 237将主燃室 210完全包围, 主燃室的炉壁 205不外 露在空气中。 烟气燃烧室的外壁 237包括隔热材料, 以防止热量散失。 The outer wall 237 of the flue gas combustion chamber completely encloses the main combustion chamber 210, and the furnace wall 205 of the main combustion chamber is not exposed to the air. The outer wall 237 of the flue gas combustion chamber includes an insulating material to prevent heat loss.
烟气在烟气燃烧室中停留的时间越长, 燃烧越充分, 二噁英等有害成分 就去除得越彻底。 因此, 在如图 2和 3所示的实施例中, 烟气燃烧通道 230 包括了下行的第一部分 231和上行的第二部分 232。 其总长度约等于主燃室 竖直高度的两倍。 但是, 只要保证进烟口至排烟口之间的烟气流经的路径长 度足够长, 如至少大于所述主燃室的竖直高度, 烟气燃烧通道的设置并不仅 限于直线形的。如图 4示出了沿主燃室 210的外周螺旋形设置的烟气燃烧通 道, 其中螺旋升角越小, 则烟气燃烧通道的长度越长, 烟气流经的路径就越 长。 The longer the smoke stays in the flue gas combustion chamber, the more complete the combustion, and the more thorough the harmful components such as dioxins are removed. Thus, in the embodiment illustrated in Figures 2 and 3, the flue gas combustion passage 230 includes a descending first portion 231 and an upward second portion 232. Its total length is approximately equal to twice the vertical height of the main combustion chamber. However, as long as the path length of the flue gas flow between the inlet to the exhaust port is sufficiently long, such as at least greater than the vertical height of the main combustion chamber, the arrangement of the flue gas combustion passage is not limited to a straight line. 4 shows a flue gas combustion passage spirally disposed along the outer circumference of the main combustion chamber 210, wherein the smaller the helix angle, the longer the length of the flue gas combustion passage, and the more the path of the flue gas flow Long.
尽管图 2-3及图 4所示的实施例中都仅示出了一条烟气燃烧通道, 在本 发明中, 烟气燃烧室可以包括多个烟气燃烧通道。 如图 5示出了本发明热解 气化炉的另一个实施例的横截面图,其中烟气燃烧室外壁和主燃室炉壁之间 设置有四个(当然还可以是更多个)轴向延伸的隔板, 从而形成四个截面为 扇形 (面积两大两小)的隔室, 其中相对两个扇形的面积相等。 这些隔室的 下部连通, 每个隔室设置对应的进烟口或排烟口, 从而形成两个从进烟口向 下延伸到隔室下部的截面面积较 d、的烟气燃烧通道第一部分和两个从隔室 下部向上延伸到排烟口的截面面积较大的烟气燃烧通道第二部分, 即形成两 条烟气燃烧通道。 Although only one flue gas combustion passage is shown in the embodiments shown in Figures 2-3 and 4, in the present invention, the flue gas combustion chamber may include a plurality of flue gas combustion passages. Figure 5 is a cross-sectional view showing another embodiment of the pyrolysis gasification furnace of the present invention, wherein four (and of course more) are disposed between the flue gas combustion outdoor wall and the main combustion chamber wall. An axially extending partition, thereby forming four compartments having a sectoral shape (two large and two small in area), wherein the areas of the two sectors are equal. The lower portions of the compartments are connected, and each compartment is provided with a corresponding inlet or exhaust vent, thereby forming two first portions of the flue gas combustion passage extending from the inlet to the lower portion of the compartment. And two portions of the flue gas combustion passage having a larger cross-sectional area extending from the lower portion of the compartment to the exhaust vent, forming two flue gas combustion passages.
尽管烟气燃烧室的外壁可以为圓筒形, 也可以是其他形状, 如图 6所示, 在其他部分结构与图 5实施例相同的情况下, 为保证烟气燃烧通道第二部分 的截面面积足够大, 可以加大相对扇形外圓的直径, 从而烟气燃烧室的外壁 有凸耳, 而并非均匀的圓筒。 Although the outer wall of the flue gas combustion chamber may be cylindrical, it may have other shapes, as shown in Fig. 6, in the same manner as the other parts of the embodiment of Fig. 5, in order to ensure the cross section of the second portion of the flue gas combustion passage. The area is large enough to increase the diameter of the outer sector of the sector, so that the outer wall of the flue gas combustion chamber has lugs instead of a uniform cylinder.
为了充分保证主燃室和烟气燃烧室之间的能量互相传导和利用, 优选的 是烟气燃烧室将主燃室完全包围而形成, 使主燃室的炉壁不外露在空气中, 从而可以充分发挥主燃室的炉壁蓄热传热的作用, 如图中各实施例所示。 In order to fully ensure the mutual conduction and utilization of energy between the main combustion chamber and the flue gas combustion chamber, it is preferred that the flue gas combustion chamber completely surrounds the main combustion chamber so that the furnace wall of the main combustion chamber is not exposed to the air, thereby The heat storage and heat transfer of the furnace wall of the main combustion chamber can be fully utilized, as shown in the various embodiments of the drawings.
另外,在烟气燃烧通道上可以设置多个送风孔,如图 2所示的送风孔 237、 238。 这些送风孔可以包括多个, 设置成在垂直于烟气流经路径的方向上送 风而形成均勾的空气流。 烟气在流经这些送风孔时, 与经送风孔流入的外界 新鲜空气混合而进一步充分燃烧, 从而使烟气中的有害物质彻底分解。 上述 送风孔的数量和具体位置并不限于图中所示, 本领域技术人员可以根据垃圾 处理量、 热解气化炉的尺寸等具体情况计算得出。 In addition, a plurality of air blowing holes may be provided in the flue gas combustion passage, such as the air blowing holes 237, 238 shown in Fig. 2. The air vents may include a plurality of air streams that are arranged to be blown in a direction perpendicular to the path of the smoke flow to form a uniform hook. When the flue gas flows through the air blowing holes, it mixes with the fresh air flowing in through the air blowing holes to further fully burn, so that the harmful substances in the flue gas are completely decomposed. The number and specific position of the above air blowing holes are not limited to those shown in the drawings, and those skilled in the art can calculate the specific conditions such as the amount of waste disposal, the size of the pyrolysis gasifier, and the like.
以上所述, 仅为本发明的具体实施方式, 但本发明的保护范围并不局限 于此, 任何熟悉本技术领域的技术人员在本发明揭露的技术范围内, 可轻易 想到变化或替换, 都应涵盖在本发明的保护范围之内。 因此, 本发明的保护 范围应所述以权利要求的保护范围为准。 The above is only the specific embodiment of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art can easily think of changes or substitutions within the technical scope of the present invention. It should be covered by the scope of the present invention. Therefore, the scope of the invention should be determined by the scope of the claims.
Claims
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
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| MX2013013660A MX2013013660A (en) | 2012-01-18 | 2012-01-18 | Garbage pyrolyzing and gasifying furnace. |
| PCT/CN2012/070531 WO2013107006A1 (en) | 2012-01-18 | 2012-01-18 | Garbage pyrolyzing and gasifying furnace |
| ES201390013U ES1111230Y (en) | 2012-01-18 | 2012-01-18 | OVEN OF GASIFICATION BY WASTE PAYROLYSIS. |
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| PCT/CN2012/070531 WO2013107006A1 (en) | 2012-01-18 | 2012-01-18 | Garbage pyrolyzing and gasifying furnace |
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| WO2013107006A1 true WO2013107006A1 (en) | 2013-07-25 |
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| PCT/CN2012/070531 Ceased WO2013107006A1 (en) | 2012-01-18 | 2012-01-18 | Garbage pyrolyzing and gasifying furnace |
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| MX (1) | MX2013013660A (en) |
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| CN108458347A (en) * | 2018-02-11 | 2018-08-28 | 蒯进永 | One kind being used for villages and small towns environmental-protection treatment device for domestic garbage |
| CN111828991A (en) * | 2020-07-10 | 2020-10-27 | 未名合一生物环保有限公司通道分公司 | A kind of waste gas combustion treatment device with folding multi-stage swirl oxidation function |
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| CN101165403A (en) * | 2006-10-20 | 2008-04-23 | 北京紫光泰和通环保技术有限公司 | Vertical daily garbage incinerator |
| JP2010276201A (en) * | 2009-05-26 | 2010-12-09 | Meiho Eco Techno:Kk | Swivel combustion furnace and combustion method |
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| CN108130131A (en) * | 2017-12-26 | 2018-06-08 | 农业部规划设计研究院 | A kind of biomass pyrogenation gasification cooking stove |
| CN108458347A (en) * | 2018-02-11 | 2018-08-28 | 蒯进永 | One kind being used for villages and small towns environmental-protection treatment device for domestic garbage |
| CN111828991A (en) * | 2020-07-10 | 2020-10-27 | 未名合一生物环保有限公司通道分公司 | A kind of waste gas combustion treatment device with folding multi-stage swirl oxidation function |
Also Published As
| Publication number | Publication date |
|---|---|
| ES1111230Y (en) | 2014-08-29 |
| ES1111230U (en) | 2014-06-06 |
| MX2013013660A (en) | 2014-08-01 |
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