CN204897822U - A biomass pyrolysis carbonization equipment based on the integrated system of gasifier and boiler - Google Patents
A biomass pyrolysis carbonization equipment based on the integrated system of gasifier and boiler Download PDFInfo
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- 238000000197 pyrolysis Methods 0.000 title claims abstract description 66
- 239000002028 Biomass Substances 0.000 title claims abstract description 65
- 238000003763 carbonization Methods 0.000 title abstract description 78
- 239000007789 gas Substances 0.000 claims abstract description 46
- 238000010438 heat treatment Methods 0.000 claims abstract description 38
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000003546 flue gas Substances 0.000 claims abstract description 25
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 26
- 229910052742 iron Inorganic materials 0.000 claims description 13
- 238000007670 refining Methods 0.000 claims description 2
- 238000007789 sealing Methods 0.000 claims description 2
- 239000003517 fume Substances 0.000 claims 8
- 238000010000 carbonizing Methods 0.000 claims 3
- 238000002309 gasification Methods 0.000 abstract description 10
- 239000002737 fuel gas Substances 0.000 abstract 2
- 230000010354 integration Effects 0.000 abstract 1
- 238000000034 method Methods 0.000 description 16
- 239000003610 charcoal Substances 0.000 description 15
- 238000002485 combustion reaction Methods 0.000 description 14
- 238000009826 distribution Methods 0.000 description 14
- 239000000463 material Substances 0.000 description 13
- 230000001105 regulatory effect Effects 0.000 description 9
- 239000000779 smoke Substances 0.000 description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 6
- 229910052799 carbon Inorganic materials 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 238000001035 drying Methods 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 229920002488 Hemicellulose Polymers 0.000 description 2
- 229920002678 cellulose Polymers 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 229920005610 lignin Polymers 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000002023 wood Substances 0.000 description 2
- 206010021143 Hypoxia Diseases 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000012263 liquid product Substances 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
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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
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
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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
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Abstract
Description
技术领域 technical field
本实用新型属于生物质能源利用技术领域,特别涉及到一种生物质热解炭化设备。 The utility model belongs to the technical field of biomass energy utilization, in particular to biomass pyrolysis and carbonization equipment.
背景技术 Background technique
炭是工业生产和日常生活中基本的能源之一,近年来由于需求量的增加,林业部门为保护森林资源和生态平衡,禁止乱砍滥伐及成材烧炭,使得木炭供需矛盾日趋紧张。于是生物质炭应运而生,有效缓解了木炭供应紧张的局势。生物质炭与传统木炭相比,具有以下优点:以废弃物为原料来代替木材,变废为宝,化害为利,有利于保护森林资源及维持生态平衡,减轻对环境的污染。 Charcoal is one of the basic energy sources in industrial production and daily life. In recent years, due to the increase in demand, the forestry department has prohibited deforestation and burning charcoal in order to protect forest resources and ecological balance, making the contradiction between supply and demand of charcoal increasingly tense. So biochar came into being, effectively alleviating the tense supply of charcoal. Compared with traditional charcoal, biochar has the following advantages: use waste as raw material instead of wood, turn waste into treasure, turn harm into profit, help protect forest resources and maintain ecological balance, and reduce environmental pollution.
生物质热解炭化设备包括两种类型,即窑式热解炭化炉和固定床式热解炭化反应炉。其中窑式热解炭化炉是在传统土窑炭化工艺基础上发展的新炉型,在产炭的同时可以回收热解过程中的气液产物,目前国内外对窑式炭化炉体研究主要集中在利用现代化工艺和制造手段改进传统炉体上,已出现很多窑式炭化炉专利。该种制炭方式对温升不易控制,以经验操作为主,制炭质量难以达到最佳,并以燃烧一部分煤炭或木材以实现外加热。制炭场所只能在野外,增加了原料与产品的运输成本,而且制炭热解气只能排放,造成了能量的浪费。 Biomass pyrolysis carbonization equipment includes two types, namely kiln type pyrolysis carbonization furnace and fixed bed type pyrolysis carbonization reaction furnace. Among them, the kiln-type pyrolysis carbonization furnace is a new type of furnace developed on the basis of the traditional earth kiln carbonization process. It can recover the gas-liquid products in the pyrolysis process while producing carbon. At present, the research on the kiln-type carbonization furnace at home and abroad mainly focuses on There have been many kiln-type carbonization furnace patents on the use of modern technology and manufacturing methods to improve the traditional furnace body. This kind of charcoal making method is not easy to control the temperature rise, and the operation is mainly based on experience, and the quality of charcoal making is difficult to achieve the best, and a part of coal or wood is burned to achieve external heating. The charcoal production site can only be in the wild, which increases the transportation cost of raw materials and products, and the charcoal pyrolysis gas can only be discharged, resulting in a waste of energy.
上世纪70年代开始,生物质固定床热解炭化技术得到迅猛发展,各种炭化炉炉型结构大量出现。生物质固定床式热解炭化反应设备的优点是运动部件少、制造简单、成本低、操作方便,可通过改变烟道和排烟口位置及处理顶部密封结构来影响气流流动从而达到热解反应稳定、得炭率高的目的,更适合于小规模制炭。 Since the 1970s, biomass fixed bed pyrolysis and carbonization technology has developed rapidly, and various carbonization furnace structures have appeared in large numbers. The advantages of biomass fixed bed pyrolysis and carbonization reaction equipment are fewer moving parts, simple manufacture, low cost, and convenient operation. The air flow can be affected by changing the position of the flue and the exhaust port and the top sealing structure to achieve the pyrolysis reaction. For the purpose of stability and high carbon yield, it is more suitable for small-scale carbon production.
固定床式炭化设备按照传热方式的不同又可分为外燃料加热式和内燃式: Fixed bed carbonization equipment can be divided into external fuel heating type and internal combustion type according to different heat transfer methods:
外加热式固定床热解炭化系统包含加热炉和热解炉两部分,由外加热炉体向热解炉提供热解所需能量。加热炉多采用管式炉,其最大优点是温度控制方便、精确,可提高生物质能源利用率,改进热解产品质量,但需消耗其它形式的能源。 The externally heated fixed bed pyrolysis and carbonization system consists of two parts: a heating furnace and a pyrolysis furnace. The external heating furnace body provides the energy required for pyrolysis to the pyrolysis furnace. Most of the heating furnaces use tube furnaces. The biggest advantage is that the temperature control is convenient and accurate, which can increase the utilization rate of biomass energy and improve the quality of pyrolysis products, but it needs to consume other forms of energy.
内燃式固定床热解炭化炉的燃烧方式类似于传统的窑式炭化炉,需在炉内点燃生物质燃料,依靠燃料自身燃烧所提供的热量维持热解。内燃式炭化炉与外热式的最大区别是热量传递方式的不同,外热式为热传导,而内燃式炭化炉是热传导、热对流、热辐射三种传递方式的组合。内燃式固定床热解炭化炉热解过程不消耗任何外加热量,反应本身和原料干燥均利用生物质自身产热,热效率较高,但生物质物料消耗较大,且为了维持热解的缺氧环境,燃烧不充分,升温速率较缓慢,热解过程中温升不易控制。 The combustion method of the internal-combustion fixed-bed pyrolysis carbonization furnace is similar to that of the traditional kiln-type carbonization furnace. Biomass fuel needs to be ignited in the furnace, and the pyrolysis is maintained by the heat provided by the fuel itself. The biggest difference between the internal combustion type carbonization furnace and the external heating type is the difference in heat transfer mode. The external heating type is heat conduction, while the internal combustion type carbonization furnace is a combination of heat conduction, heat convection, and heat radiation. The pyrolysis process of the internal combustion fixed bed pyrolysis carbonization furnace does not consume any external heat. Both the reaction itself and the drying of raw materials use the heat generated by the biomass itself. The thermal efficiency is high, but the consumption of biomass materials is large, and in order to maintain the oxygen deficiency Environment, insufficient combustion, slow heating rate, difficult to control temperature rise during pyrolysis.
随着国家对生物质能源关注度的不断提高,生物质热解制炭产业必将得到快速广阔的发展。热解炭化机理以及高效、节能、稳定且具有较高自动化、机械化水平的生物质热解炭化反应设备将是未来的主要研究方向。 With the continuous improvement of the country's attention to biomass energy, the biomass pyrolysis charcoal industry will surely develop rapidly and broadly. The mechanism of pyrolysis and carbonization and biomass pyrolysis and carbonization reaction equipment with high efficiency, energy saving, stability and high level of automation and mechanization will be the main research directions in the future.
发明内容 Contents of the invention
本实用新型的目的是提出一种基于气化炉与锅炉一体化系统的生物质热解炭化设备,以充分利用生物质热解所产生的能量,达到节能目的。 The purpose of this utility model is to propose a biomass pyrolysis carbonization equipment based on the integrated system of gasifier and boiler, so as to make full use of the energy generated by biomass pyrolysis and achieve the purpose of energy saving.
本实用新型的基于气化炉与锅炉一体化系统的生物质热解炭化设备,由生物质炭化炉、生物质气化炉和锅炉组成,关键在于所述生物质炭化炉由炉体、盖板和架设于炉体内部上方的内锅构成,所述炉体设有烟气排放口,所述盖板密封扣合于炉体上,盖板与炉体形成加热腔,盖板与内锅形成炭化腔,所述盖板对应于内锅上方的位置处设有可开启及关闭的湿气排放口;所述内锅底面与加热腔的底壁之间形成炭化炉炉膛,所述炉膛内放置有燃烧器;所述炭化腔通过热解气通道与锅炉的燃烧器连接;所述生物质气化炉的燃气出口通过燃气通道分别与生物质炭化炉的燃烧器及锅炉的燃烧器连接。 The biomass pyrolysis and carbonization equipment based on the integrated system of gasification furnace and boiler of the utility model is composed of a biomass carbonization furnace, a biomass gasification furnace and a boiler. The key is that the biomass carbonization furnace consists of a furnace body and a cover plate It is composed of an inner pot erected above the inside of the furnace body, the furnace body is provided with a flue gas discharge port, the cover plate is sealed and buckled on the furnace body, the cover plate and the furnace body form a heating chamber, and the cover plate and the inner pot form a In the carbonization chamber, the cover plate is provided with an openable and closable moisture discharge port corresponding to the position above the inner pot; a carbonization furnace furnace is formed between the bottom surface of the inner pot and the bottom wall of the heating chamber, and the furnace chamber is placed There is a burner; the carbonization chamber is connected to the burner of the boiler through the pyrolysis gas channel; the gas outlet of the biomass gasification furnace is respectively connected to the burner of the biomass carbonization furnace and the burner of the boiler through the gas channel.
气化炉生产可燃气供给锅炉燃烧,并将小部分可燃气分流给炭化炉燃烧,从而给内锅加热,内锅里面放置的生物质材料棒在炭化热解阶段产生的热解气供给锅炉燃烧。在热解气产生期间,气化炉可以以最低输出的模式运行,以达到节能目的。 The combustible gas produced by the gasification furnace is supplied to the boiler for combustion, and a small part of the combustible gas is diverted to the carbonization furnace for combustion, thereby heating the inner pot, and the pyrolysis gas generated by the biomass material rods placed in the inner pot during the carbonization and pyrolysis stage is supplied to the boiler for combustion . During the generation of pyrolysis gas, the gasifier can be operated at the lowest output mode to save energy.
生物质炭化炉的燃烧器在燃烧时产生的烟气通过炉体的烟气排放口排出。 The flue gas produced by the burner of the biomass carbonization furnace is discharged through the flue gas discharge port of the furnace body.
在对内锅加热的过程中,生物质材料棒受热而温度逐渐升高,具体分为下述几个阶段:温度在200℃以下时,此过程基本为干燥过程,生物质材料棒中所含水分依靠外部供给的热量而蒸发,并由盖板的湿气排放口排出;当温度继续升高,达到200~400℃的时候,生物质材料棒的主要构成纤维素、半纤维素、木质素开始发生热分解并释放出热解气,并沿着热解气通道输送至锅炉的燃烧器供锅炉燃烧(此时需要关闭盖板的湿气排放口),伴随着此过程生物质材料棒的质量开始大幅度减少,纤维素、半纤维素、木质素的主要热分解反应在450~500℃时终止;当温度达到500℃以上的时候,生物质炭处于精炼过程,在产生H2的同时,炭中的炭元素形成缩合多环芳香族结果,炭元素的比例超过80%。 In the process of heating the inner pot, the biomass material rod is heated and the temperature gradually rises, which is divided into the following stages: when the temperature is below 200°C, this process is basically a drying process, and the biomass material rod contains Moisture is evaporated by external heat and discharged from the moisture outlet of the cover plate; when the temperature continues to rise and reaches 200~400°C, the main components of biomass material rods are cellulose, hemicellulose, and lignin. The pyrolysis begins to occur and the pyrolysis gas is released, which is transported to the burner of the boiler along the pyrolysis gas channel for combustion in the boiler (at this time, the moisture discharge port of the cover needs to be closed), along with the process of biomass material sticks The quality begins to decrease significantly, and the main thermal decomposition reactions of cellulose, hemicellulose, and lignin are terminated at 450~500°C; when the temperature reaches above 500°C, the biochar is in the refining process, and while generating H 2 , The carbon element in the charcoal forms a condensed polycyclic aromatic result, and the proportion of the carbon element exceeds 80%.
进一步地,所述烟气排放口有多个,并均匀分布于炉体的侧壁,所述炉体设有若干个温度传感器,以探测加热腔的温度分布情况;所述每个烟气排放口均设有用于改变烟气排放口开度的烟气排放调节阀;所述温度传感器、烟气排放调节阀均与一个控制单元电连接,所述控制单元根据温度传感器的信息来控制烟气排放调节阀的开度。在炭化作业过程中,控制单元接收温度传感器的信号,以此来判断加热腔的温度分布情况,如果加热腔的温度分布不够均匀,那么控制单元就控制温度较高处的烟气排放调节阀增大开度,或者控制温度较低处的烟气排放调节阀减小开度,从而调整加热腔的温度分布,使得加热腔内温度分布均匀,改善炭化质量。 Further, there are multiple flue gas discharge ports, which are evenly distributed on the side wall of the furnace body, and the furnace body is provided with several temperature sensors to detect the temperature distribution of the heating chamber; each of the flue gas discharge Each port is equipped with a flue gas discharge regulating valve for changing the opening of the flue gas discharge port; the temperature sensor and the flue gas discharge regulating valve are electrically connected to a control unit, and the control unit controls the flue gas discharge according to the information of the temperature sensor. The opening of the discharge regulating valve. During the carbonization process, the control unit receives the signal from the temperature sensor to judge the temperature distribution of the heating chamber. Large opening, or control the flue gas discharge regulating valve at a lower temperature to reduce the opening, thereby adjusting the temperature distribution of the heating chamber, making the temperature distribution in the heating chamber uniform and improving the carbonization quality.
进一步地,所述烟气排放口与一个烟气排放管道连接,所述烟气排放管道设有抽风机,所述抽风机与控制单元电连接。通过一个统一的烟气排放管道来排放烟气,有助于控制污染,而且抽风机可以通过调节排气功率,进而影响加热腔的温度------当抽风机的排气功率较大时,加热腔内的热气排出速度较快,带走加热腔内的热量的速度较快,加热腔的温度就会降低,反之,加热腔的温度就会升高。 Further, the smoke discharge port is connected to a smoke discharge pipe, and the smoke discharge pipe is provided with an exhaust fan, and the exhaust fan is electrically connected to the control unit. Discharging the flue gas through a unified flue gas discharge pipe helps to control pollution, and the exhaust fan can adjust the exhaust power to affect the temperature of the heating chamber ------ when the exhaust power of the exhaust fan is large At this time, the hot gas in the heating chamber is discharged faster, and the heat in the heating chamber is taken away faster, and the temperature of the heating chamber will decrease, otherwise, the temperature of the heating chamber will increase.
进一步地,所述热解气通道设有热解气净化装置,以净化炭化腔排出的热解气,减少其内部所含焦油等物质对锅炉燃烧器的不利影响。 Further, the pyrolysis gas channel is provided with a pyrolysis gas purification device to purify the pyrolysis gas discharged from the carbonization chamber and reduce the adverse effects of tar and other substances contained in it on the boiler burner.
进一步地,所述热解气通道设有与控制单元电连接的阀门,这样可以在炭化作业的初始阶段(即生物质材料棒的干燥过程)关闭阀门,避免湿气进入到锅炉内,而只在生物质材料棒热解时打开阀门,使得进入到锅炉燃烧器内的热解气纯净。 Further, the pyrolysis gas channel is provided with a valve electrically connected to the control unit, so that the valve can be closed at the initial stage of the carbonization operation (that is, the drying process of the biomass material rod) to prevent moisture from entering the boiler, and only When the biomass material rod is pyrolyzed, the valve is opened to make the pyrolysis gas entering the boiler burner pure.
进一步地,所述炭化腔内设有若干个热电偶,以探测炭化腔内的温度分布情况,以便于控制单元根据炭化腔内的温度分布情况来控制其它部件的工作,尽量使得炭化腔内的温度分布均匀。 Further, several thermocouples are provided in the carbonization chamber to detect the temperature distribution in the carbonization chamber, so that the control unit can control the work of other components according to the temperature distribution in the carbonization chamber, so as to make the temperature in the carbonization chamber Even temperature distribution.
进一步地,所述炭化腔内放置有若干个顶部开口的铁笼框,且相邻铁笼框之间留有间隙。将生物质材料棒竖直放入铁笼框内,然后再将铁笼框放入到内锅内,炭锅内可放入多层多个铁笼框,每层之间留有空间,利用炭化腔内的热传输而达到温度平衡。 Further, several iron cage frames with open tops are placed in the carbonization chamber, and gaps are left between adjacent iron cage frames. Put the biomass material rods vertically into the iron cage frame, and then put the iron cage frame into the inner pot. Multiple layers of iron cage frames can be placed in the charcoal pot, leaving space between each layer. The heat transfer in the carbonization chamber achieves temperature balance.
本实用新型的生物质热解炭化设备依附于气化炉和锅炉而设置,可在市内甚至工业区制炭,零排放无污染。用气化炉生产的可燃气实现外加热,外加热成本极低。炭化过程产生的热解气返给锅炉燃烧,实现了能源利用的最大化,达到了节能目的。在制炭过程中,炭化腔内的升温可以得到有效监控,因此炭化过程的工艺曲线可由程序控制实现,降低了对工人经验的依赖,炭化质量有保证。 The biomass pyrolysis and carbonization equipment of the utility model is attached to a gasification furnace and a boiler, and can make carbon in the city or even in an industrial area, with zero emission and no pollution. The combustible gas produced by the gasifier is used for external heating, and the cost of external heating is extremely low. The pyrolysis gas generated during the carbonization process is returned to the boiler for combustion, which maximizes energy utilization and achieves the purpose of energy saving. During the carbonization process, the temperature rise in the carbonization chamber can be effectively monitored, so the process curve of the carbonization process can be realized by program control, which reduces the dependence on the experience of workers and ensures the quality of carbonization.
附图说明 Description of drawings
图1是本实用新型的生物质热解炭化设备的结构图。 Fig. 1 is a structural diagram of the biomass pyrolysis carbonization equipment of the present invention.
图2是本实用新型的生物质热解炭化设备的俯视图(未包括盖板)。 Fig. 2 is a top view of the biomass pyrolysis and carbonization equipment of the present invention (without the cover plate).
附图说明:1、生物质炭化炉;11、炉体;12、盖板;13、内锅;14、烟气排放口;15、温度传感器;16、湿气排放口;17、燃烧器;18、烟气排放管道;19、铁笼框;2、生物质气化炉;3、锅炉;4、热解气通道;5、热解气净化装置;6、阀门;7、燃气通道;8、管道阀。 Description of drawings: 1. Biomass carbonization furnace; 11. Furnace body; 12. Cover plate; 13. Inner pot; 14. Smoke discharge port; 15. Temperature sensor; 16. Moisture discharge port; 17. Burner; 18. Flue gas discharge pipe; 19. Iron cage frame; 2. Biomass gasifier; 3. Boiler; 4. Pyrolysis gas channel; 5. Pyrolysis gas purification device; 6. Valve; 7. Gas channel; 8 , Pipeline valve.
具体实施方式 Detailed ways
下面对照附图,通过对实施实例的描述,对本实用新型的具体实施方式如所涉及的各构件的形状、构造、各部分之间的相互位置及连接关系、各部分的作用及工作原理等作进一步的详细说明。 Below with reference to the accompanying drawings, through the description of the implementation examples, the specific embodiments of the present utility model, such as the shape, structure, mutual position and connection relationship between each part, the role and working principle of each part, etc. Further details.
实施例1: Example 1:
如图所示,本实施例的基于气化炉与锅炉一体化系统的生物质热解炭化设备由生物质炭化炉1、生物质气化炉2和锅炉3组成,关键在于所述生物质炭化炉1由炉体11、盖板12和架设于炉体11内部上方的内锅13构成,所述炉体11的两侧侧壁均匀设有多个烟气排放口14,每个烟气排放口14均设有用于改变烟气排放口14开度的烟气排放调节阀;炉体11内还设有若干个温度传感器15,以探测加热腔的温度分布情况;所述温度传感器15、烟气排放调节阀均与一个控制单元电连接,所述控制单元根据温度传感器15的信息来控制烟气排放调节阀的工作。 As shown in the figure, the biomass pyrolysis and carbonization equipment based on the integrated system of gasifier and boiler in this embodiment is composed of biomass carbonization furnace 1, biomass gasification furnace 2 and boiler 3. The key lies in the biomass carbonization The furnace 1 is composed of a furnace body 11, a cover plate 12 and an inner pot 13 erected above the interior of the furnace body 11. The side walls on both sides of the furnace body 11 are evenly provided with a plurality of smoke discharge ports 14, and each smoke discharge The openings 14 are all provided with flue gas discharge regulating valves for changing the opening degree of the flue gas discharge port 14; several temperature sensors 15 are also provided in the furnace body 11 to detect the temperature distribution of the heating chamber; the temperature sensors 15, the flue gas The gas discharge regulating valves are all electrically connected to a control unit, and the control unit controls the operation of the flue gas discharge regulating valves according to the information of the temperature sensor 15 .
所述盖板12利用水隔密封的方式扣合于炉体11上,盖板12与炉体11形成加热腔,内锅13位于加热腔内,盖板12与内锅13形成炭化腔,所述盖板12对应于内锅13上方的位置处设有可开启及关闭的湿气排放口16;所述内锅13底面与加热腔的底壁之间形成炭化炉炉膛,所述炉膛内放置有若干个燃烧器17;所述炭化腔通过热解气通道4与锅炉3的燃烧器17连接,热解气通道4设有热解气净化装置5,以净化炭化腔排出的热解气,热解气通道4的入口处设有与控制单元电连接的阀门6;所述生物质气化炉2的燃气出口通过燃气通道7分别与生物质炭化炉1的燃烧器17及锅炉3的燃烧器17连接,且燃气通道7设有管道阀8,以用于分配输送给生物质炭化炉1的燃烧器17及锅炉3的燃烧器17的燃气量。 The cover plate 12 is buckled on the furnace body 11 in a water-tight manner. The cover plate 12 and the furnace body 11 form a heating chamber, the inner pot 13 is located in the heating chamber, and the cover plate 12 and the inner pot 13 form a carbonization chamber. The cover plate 12 is provided with an openable and closable moisture discharge port 16 corresponding to the position above the inner pot 13; a carbonization furnace hearth is formed between the bottom surface of the inner pot 13 and the bottom wall of the heating chamber, and the There are several burners 17; the carbonization chamber is connected to the burner 17 of the boiler 3 through the pyrolysis gas passage 4, and the pyrolysis gas passage 4 is provided with a pyrolysis gas purification device 5 to purify the pyrolysis gas discharged from the carbonization chamber, The entrance of the pyrolysis gas channel 4 is provided with a valve 6 electrically connected to the control unit; the gas outlet of the biomass gasification furnace 2 is connected to the burner 17 of the biomass carbonization furnace 1 and the combustion of the boiler 3 through the gas channel 7 respectively. Connected to the burner 17, and the gas channel 7 is provided with a pipeline valve 8 for distributing the amount of gas delivered to the burner 17 of the biomass carbonization furnace 1 and the burner 17 of the boiler 3 .
烟气排放口14与一个烟气排放管道18连接,所述烟气排放管道18设有抽风机,所述抽风机与控制单元电连接。 The smoke discharge port 14 is connected with a smoke discharge pipe 18, and the smoke discharge pipe 18 is provided with an exhaust fan, and the exhaust fan is electrically connected with the control unit.
炭化腔内分高、中、低三个高度布置有若干个热电偶(图中未画出热电偶),以探测炭化腔内的温度分布情况,以便于控制单元根据炭化腔内的温度分布情况来控制其它部件的工作,尽量使得炭化腔内的温度分布均匀。 Several thermocouples are arranged in the carbonization chamber at high, middle and low heights (thermocouples are not shown in the figure) to detect the temperature distribution in the carbonization chamber so that the control unit can To control the work of other components, try to make the temperature distribution in the carbonization chamber even.
炭化腔内放置有若干个顶部开口的铁笼框19,且相邻铁笼框19之间留有间隙。将生物质材料棒竖直放入铁笼框19内,然后再将铁笼框19放入到内锅13内,炭锅内可放入多层多个铁笼框19,每层之间留有空间,利用炭化腔内的热传输而达到温度平衡。 Several iron cage frames 19 with open tops are placed in the carbonization chamber, and gaps are left between adjacent iron cage frames 19 . Put the biomass material rod vertically into the iron cage frame 19, then put the iron cage frame 19 into the inner pot 13, and put multiple layers of multiple iron cage frames 19 in the charcoal pot, leaving space between each layer. There is room to achieve temperature balance by utilizing heat transfer in the carbonization chamber.
气化炉生产可燃气供给锅炉3燃烧,并将小部分可燃气分流给炭化炉燃烧,从而给内锅13加热,内锅13里面放置的生物质材料棒在炭化热解阶段产生的热解气供给锅炉3燃烧。在热解气产生期间,锅炉主要依靠热解气来工作,气化炉可以以最低输出的模式运行,以达到节能目的。 The combustible gas produced by the gasification furnace is supplied to the boiler 3 for combustion, and a small part of the combustible gas is diverted to the carbonization furnace for combustion, thereby heating the inner pot 13, and the pyrolysis gas generated by the biomass material sticks placed in the inner pot 13 during the carbonization pyrolysis stage Supply boiler 3 to burn. During the generation of pyrolysis gas, the boiler mainly relies on pyrolysis gas to work, and the gasifier can be operated in the mode of the lowest output to achieve the purpose of energy saving.
生物质炭化炉1的燃烧器17在燃烧时产生的烟气通过炉体11的烟气排放口14排出。生物质炭化炉1的加热腔由燃气供给控制升温,由烟气排量控制降温。在炭化作业过程中,控制单元接收温度传感器15的信号,以此来判断加热腔的温度分布情况,如果加热腔的温度分布不够均匀,那么控制单元就控制温度较高处的烟气排放调节阀增大开度,或者控制温度较低处的烟气排放调节阀减小开度,从而调整加热腔的温度分布,使得加热腔内温度分布均匀,改善炭化质量。 The flue gas produced by the burner 17 of the biomass carbonization furnace 1 is discharged through the flue gas discharge port 14 of the furnace body 11 . The heating chamber of the biomass carbonization furnace 1 is controlled by the gas supply to increase the temperature, and the temperature is controlled by the flue gas discharge. During the carbonization process, the control unit receives the signal from the temperature sensor 15 to judge the temperature distribution of the heating chamber. If the temperature distribution of the heating chamber is not uniform enough, the control unit controls the flue gas discharge regulating valve at the higher temperature Increase the opening degree, or control the flue gas discharge regulating valve at a lower temperature to reduce the opening degree, thereby adjusting the temperature distribution of the heating chamber, making the temperature distribution in the heating chamber uniform, and improving the carbonization quality.
在炭化作业的初始阶段(即生物质材料棒的干燥过程)关闭热解气通道4的入口处的阀门6,并打开湿气排放口16,避免湿气进入到锅炉3的燃烧器17内;在生物质材料棒的热解时打开热解气通道4的入口处的阀门6,关闭湿气排放口16,使得进入到锅炉3燃烧器17内的热解气纯净。 In the initial stage of the carbonization operation (that is, the drying process of the biomass material rod), close the valve 6 at the entrance of the pyrolysis gas channel 4, and open the moisture discharge port 16 to prevent moisture from entering the burner 17 of the boiler 3; Open the valve 6 at the entrance of the pyrolysis gas channel 4 during the pyrolysis of the biomass material rod, and close the moisture discharge port 16, so that the pyrolysis gas entering the burner 17 of the boiler 3 is pure.
传统制炭一个周期需要数天完成,本专利技术一个制炭周期只要24小时即可完成,大大提高了工作效率。 It takes several days to complete a traditional charcoal production cycle, but the patented technology can complete a charcoal production cycle in 24 hours, which greatly improves work efficiency.
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