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CN204897824U - A biomass pyrolysis carbonization equipment - Google Patents

A biomass pyrolysis carbonization equipment Download PDF

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Publication number
CN204897824U
CN204897824U CN201520432444.2U CN201520432444U CN204897824U CN 204897824 U CN204897824 U CN 204897824U CN 201520432444 U CN201520432444 U CN 201520432444U CN 204897824 U CN204897824 U CN 204897824U
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carbonization
cover plate
chamber
furnace body
pyrolysis
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杜海江
刘光华
王新强
李崇实
董燕萍
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Dongguan Baida New Energy Co ltd
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

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Abstract

The utility model aims at providing a living beings pyrolysis carbonization equipment to improve system charcoal quality. The biomass pyrolysis carbonization equipment of the utility model consists of a furnace body, a cover plate and an inner pot arranged above the inner part of the furnace body, wherein 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 cavity, the cover plate and the inner pot form a carbonization cavity, and the cover plate is provided with a moisture discharge port which can be opened and closed corresponding to the position above the inner pot; a hearth of the carbonization furnace is formed between the bottom surface of the inner pot and the bottom wall of the heating cavity, and a burner is placed in the hearth; the carbonization cavity is connected with a pyrolysis gas channel extending to the outside of the furnace body. The utility model discloses a living beings pyrolysis carbonization equipment is at the charcoal in-process, and the intensification in the carbomorphism intracavity can be effectively monitored, and consequently the process curve of carbomorphism process can be realized by program control, has reduced the reliance to workman's experience, and the carbomorphism quality is guaranteed.

Description

一种生物质热解炭化设备A biomass pyrolysis carbonization equipment

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。该种制炭的温升不易控制,以经验操作为主,制炭质量难以达到最佳,并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. The temperature rise of this kind of charcoal is not easy to control, and the operation is mainly based on experience. It is difficult to achieve the best quality of charcoal, 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.

炭化过程中,生物质材料棒的温度均衡并按温度曲线升温对制出炭的质量至关重要,传统制炭方法全凭人员的经验控制,无精度可言,因此一炉炭制成后,窑内不同位置的炭品质不一致,制炭质量不佳。 During the carbonization process, the temperature balance of the biomass material rods and the temperature rise according to the temperature curve are very important to the quality of the charcoal produced. The traditional charcoal production methods are all controlled by the experience of personnel, and there is no accuracy at all. Therefore, after a batch of charcoal is produced, The quality of charcoal in different positions in the kiln is inconsistent, and the quality of charcoal production is not good.

发明内容 Contents of the invention

本实用新型的目的是提出一种生物质热解炭化设备,以改善制炭质量。 The purpose of the utility model is to propose a biomass pyrolysis carbonization equipment to improve the quality of charcoal production.

本实用新型的生物质热解炭化设备由炉体、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;所述炭化腔与一个延伸至炉体外部的热解气通道连接。 The biomass pyrolysis and carbonization equipment of the utility model is composed of a furnace body, a cover plate and an inner pot erected above the inside of the furnace body. The furnace body is provided with a flue gas discharge port, and the cover plate is sealed and fastened on the furnace body , the cover plate and the furnace body form a heating chamber, the cover plate and the inner pot form a carbonization chamber, and the cover plate is provided with an openable and closable moisture discharge port corresponding to the position above the inner pot; the bottom surface of the inner pot and the heating A carbonization furnace hearth is formed between the bottom walls of the chamber, and a burner is placed in the hearth; the carbonization chamber is connected with a pyrolysis gas channel extending to the outside of the furnace body.

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。 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.

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. Exhaust the flue gas through a unified flue gas discharge pipe, which helps to control pollution, and the exhaust fan can adjust the exhaust power, which in turn affects the temperature of the heating chamber --- when the exhaust power of the exhaust fan is large , the hot air in the heating chamber is discharged faster, and the heat in the heating chamber is taken away faster, the temperature of the heating chamber will decrease, and vice versa, the temperature of the heating chamber will rise.

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,使得炭化所产生的热解气纯净。 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 produced by carbonization 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.

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.

上述生物质热解炭化设备的控制方法包括如下步骤: The control method of the above-mentioned biomass pyrolysis carbonization equipment includes the following steps:

A:将生物质材料棒放入铁笼框内,并将铁笼框放入内锅内,将盖板密封扣合于炉体上; A: Put the biomass material rods into the iron cage frame, put the iron cage frame into the inner pot, and seal the cover plate on the furnace body;

B:利用燃烧器对内锅进行加热,并利用燃烧器的燃料供给、烟气排放口的开度、以及抽风机的抽风功率来控制炭化腔内的温升速度,使炭化腔内的温升曲线符合预定曲线; B: Use the burner to heat the inner pot, and use the fuel supply of the burner, the opening of the flue gas discharge port, and the exhaust power of the exhaust fan to control the temperature rise rate in the carbonization chamber, so that the temperature rise in the carbonization chamber The curve conforms to the predetermined curve;

C:在加热过程中,利用温度传感器探测加热腔的温度分布情况,并根据加热腔、的温度分布情况来控制烟气排放口的开度,从而调节加热腔的温度分布情况,并使得加热腔的温度分布均匀。 C: During the heating process, the temperature sensor is used to detect the temperature distribution of the heating chamber, and the opening of the flue gas discharge port is controlled according to the temperature distribution of the heating chamber, so as to adjust the temperature distribution of the heating chamber and make the heating chamber The temperature distribution is even.

具体来说,所述B步骤中,所述预定曲线由下述四个阶段构成: Specifically, in the B step, the predetermined curve consists of the following four stages:

干燥阶段:以2℃/min的温升速率使炭化腔内的温度升高至130~150℃,并在130~150℃温度范围内保持4小时; Drying stage: raise the temperature in the carbonization chamber to 130-150°C at a temperature rise rate of 2°C/min, and keep it within the temperature range of 130-150°C for 4 hours;

预炭化阶段:以2℃/min的温升速率使炭化腔内的温度升高至250~275℃,并在250~275℃温度范围内保持6小时; Pre-carbonization stage: raise the temperature in the carbonization chamber to 250-275°C at a temperature rise rate of 2°C/min, and keep it within the temperature range of 250-275°C for 6 hours;

炭化阶段:以2℃/min的温升速率使炭化腔内的温度升高至375~400℃,并在375~400℃温度范围内保持10小时; Carbonization stage: raise the temperature in the carbonization chamber to 375-400°C at a temperature rise rate of 2°C/min, and keep it within the temperature range of 375-400°C for 10 hours;

煅烧阶段:以2℃/min的温升速率使炭化腔内的温度升高至450~500℃,并在450~500℃温度范围内保持2小时; Calcination stage: raise the temperature in the carbonization chamber to 450-500°C at a temperature rise rate of 2°C/min, and keep it in the temperature range of 450-500°C for 2 hours;

在干燥阶段,打开湿气排放口,并关闭热解气通道的入口处的阀门;在预炭化阶段、炭化阶段及煅烧阶段,关闭湿气排放口,并打开热解气通道的入口处的阀门; In the drying stage, open the moisture discharge port and close the valve at the entrance of the pyrolysis gas channel; in the pre-carbonization stage, carbonization stage and calcination stage, close the moisture discharge port and open the valve at the entrance of the pyrolysis gas channel ;

上述温度曲线的原理如下: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放出热解气,并沿着热解气通道输送至锅炉的燃烧器以供燃烧(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%。 The principle of the above temperature curve is as follows: In the process of heating the inner pot, the biomass material rod is heated and the temperature gradually rises, which can be divided into the following stages: when the temperature is below 200°C, this process is basically a drying process, The moisture contained in the biomass material rod is evaporated by the heat supplied from the outside, and is discharged from the moisture discharge port of the cover plate; when the temperature continues to rise and reaches 200~400°C, the main component of the biomass material rod is cellulose , hemicellulose, and lignin begin to undergo thermal decomposition and release pyrolysis gas, which is transported to the burner of the boiler along the pyrolysis gas channel for combustion (at this time, the moisture discharge port of the cover needs to be closed), accompanied by this During the process, the quality of biomass material rods 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, While generating H 2 , the carbon elements in the charcoal form condensed polycyclic aromatics. As a result, the proportion of carbon elements exceeds 80%.

所述C步骤中,如果加热腔的温度分布不均匀,则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。 In the step C, if the temperature distribution of the heating chamber is not uniform, the flue gas discharge regulating valve at a higher temperature is controlled to increase the opening, or the flue gas discharge regulating valve at a lower temperature is controlled to decrease the opening, thereby Adjust the temperature distribution of the heating chamber to make the temperature distribution in the heating chamber uniform.

本实用新型的生物质热解炭化设备在制炭过程中,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。 During the carbonization process of the biomass pyrolysis carbonization equipment of the utility model, 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、炉体;2、盖板;3、内锅;4、烟气排放口;5、温度传感器;6、湿气排放口;7、燃烧器;8、热解气通道;9、阀门;10、烟气排放管道;11、抽风机;12、铁笼框。 Description of drawings: 1. Furnace body; 2. Cover plate; 3. Inner pot; 4. Smoke discharge port; 5. Temperature sensor; 6. Moisture discharge port; 7. Burner; 8. Pyrolysis gas channel; 9. Valve; 10. Flue gas discharge pipe; 11. Exhaust fan; 12. Iron cage frame.

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,本实施例的生物质热解炭化设备由炉体1、盖板2和架设于炉体1内部上方的内锅3构成,所述炉体1的侧壁均匀设有多个烟气排放口4,每个烟气排放口4均设有用于改变烟气排放口4开度的烟气排放调节阀;炉体1内还设有若干个温度传感器5,以探测加热腔的温度分布情况;所述温度传感器5、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5的信息来控制烟气排放调节阀的开度。 As shown in the figure, the biomass pyrolysis and carbonization equipment of this embodiment is composed of a furnace body 1, a cover plate 2, and an inner pot 3 erected above the interior of the furnace body 1. The side wall of the furnace body 1 is evenly equipped with a plurality of The flue gas discharge port 4, each flue gas discharge port 4 is provided with a flue gas discharge regulating valve for changing the opening degree of the flue gas discharge port 4; several temperature sensors 5 are also provided in the furnace body 1 to detect the temperature of the heating chamber. Temperature distribution: the temperature sensor 5 and the flue gas discharge regulating valve are both electrically connected to a control unit, and the control unit controls the opening of the flue gas discharge regulating valve according to the information of the temperature sensor 5 .

所述盖板2利用水隔密封的方式扣合于炉体1上,盖板2与炉体1形成加热腔,内锅3位于加热腔内,盖板2与内锅3形成炭化腔,所述盖板2对应于内锅3上方的位置处设有可开启及关闭的湿气排放口6;所述内锅3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7;所述炭化腔与一个延伸至炉体1外部的热解气通道8连接,热解气通道8的入口处设有与控制单元电连接的阀门9。 The cover plate 2 is buckled on the furnace body 1 in a water-tight manner, the cover plate 2 and the furnace body 1 form a heating chamber, the inner pot 3 is located in the heating chamber, and the cover plate 2 and the inner pot 3 form a carbonization chamber. The cover plate 2 is provided with an openable and closable moisture discharge port 6 corresponding to the position above the inner pot 3; a carbonization furnace hearth is formed between the bottom surface of the inner pot 3 and the bottom wall of the heating chamber, and the There are several burners 7; the carbonization chamber is connected to a pyrolysis gas channel 8 extending to the outside of the furnace body 1, and a valve 9 electrically connected to the control unit is provided at the entrance of the pyrolysis gas channel 8.

烟气排放口4与一个烟气排放管道10连接,所述烟气排放管道10设有抽风机11,所述抽风机11与控制单元电连接。 The smoke discharge port 4 is connected with a smoke discharge pipe 10, and the smoke discharge pipe 10 is provided with an exhaust fan 11, and the exhaust fan 11 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12,且相邻铁笼框12之间留有间隙。将生物质材料棒竖直放入铁笼框12内,然后再将铁笼框12放入到内锅3内,炭锅内可放入多层多个铁笼框12,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 12 with top openings are placed in the carbonization chamber, and gaps are left between adjacent iron cage frames 12 . Put the biomass material rods vertically into the iron cage frame 12, then put the iron cage frame 12 into the inner pot 3, multiple layers of multiple iron cage frames 12 can be put in the charcoal pot, leave space between each layer There is room to achieve temperature balance by utilizing heat transfer in the carbonization chamber.

生物质炭化炉的燃烧器7在燃烧时产生的烟气通过炉体1的烟气排放口4排出。生物质炭化炉的加热腔由燃气供给控制升温,由烟气排量控制降温。 The flue gas generated by the burner 7 of the biomass carbonization furnace is discharged through the flue gas discharge port 4 of the furnace body 1 . The heating chamber of the biomass carbonization furnace is controlled by the gas supply to increase the temperature, and the temperature is controlled by the flue gas discharge.

具体来说,上述生物质热解炭化设备的控制方法包括如下步骤: Specifically, the control method for the above-mentioned biomass pyrolysis and carbonization equipment includes the following steps:

A:将生物质材料棒放入铁笼框12内,并将铁笼框12放入内锅3内,将盖板2密封扣合于炉体1上; A: Put the biomass material rods into the iron cage frame 12, put the iron cage frame 12 into the inner pot 3, and seal the cover plate 2 on the furnace body 1;

B:利用燃烧器7对内锅3进行加热,并利用燃烧器7的燃料供给、烟气排放口4的开度、以及抽风机11的抽风功率来控制炭化腔内的温升速度,使炭化腔内的温升曲线符合预定曲线; B: Use the burner 7 to heat the inner pot 3, and use the fuel supply of the burner 7, the opening of the flue gas discharge port 4, and the exhaust power of the exhaust fan 11 to control the temperature rise rate in the carbonization chamber to make carbonization The temperature rise curve in the cavity conforms to the predetermined curve;

C:在加热过程中,利用温度传感器5探测加热腔的温度分布情况,并根据加热腔、的温度分布情况来控制烟气排放口4的开度,从而调节加热腔的温度分布情况,并使得加热腔的温度分布均匀。 C: During the heating process, use the temperature sensor 5 to detect the temperature distribution of the heating chamber, and control the opening of the flue gas discharge port 4 according to the temperature distribution of the heating chamber, thereby adjusting the temperature distribution of the heating chamber, and making The temperature distribution in the heating chamber is uniform.

所述B步骤中,所述预定曲线由下述四个阶段构成: In the B step, the predetermined curve consists of the following four stages:

干燥阶段:以2℃/min的温升速率使炭化腔内的温度升高至130~150℃,并在130~150℃温度范围内保持4小时; Drying stage: raise the temperature in the carbonization chamber to 130-150°C at a temperature rise rate of 2°C/min, and keep it within the temperature range of 130-150°C for 4 hours;

预炭化阶段:以2℃/min的温升速率使炭化腔内的温度升高至250~275℃,并在250~275℃温度范围内保持6小时; Pre-carbonization stage: raise the temperature in the carbonization chamber to 250-275°C at a temperature rise rate of 2°C/min, and keep it within the temperature range of 250-275°C for 6 hours;

炭化阶段:以2℃/min的温升速率使炭化腔内的温度升高至375~400℃,并在375~400℃温度范围内保持10小时; Carbonization stage: raise the temperature in the carbonization chamber to 375-400°C at a temperature rise rate of 2°C/min, and keep it within the temperature range of 375-400°C for 10 hours;

煅烧阶段:以2℃/min的温升速率使炭化腔内的温度升高至450~500℃,并在450~500℃温度范围内保持2小时; Calcination stage: raise the temperature in the carbonization chamber to 450-500°C at a temperature rise rate of 2°C/min, and keep it in the temperature range of 450-500°C for 2 hours;

在干燥阶段,打开湿气排放口6,并关闭热解气通道8的入口处的阀门9;在预炭化阶段、炭化阶段及煅烧阶段,关闭湿气排放口6,并打开热解气通道8的入口处的阀门9; In the drying stage, open the moisture discharge port 6 and close the valve 9 at the entrance of the pyrolysis gas channel 8; in the pre-carbonization stage, carbonization stage and calcination stage, close the moisture discharge port 6 and open the pyrolysis gas channel 8 The inlet valve 9;

所述C步骤中,如果加热腔的温度分布不均匀,则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 In the step C, if the temperature distribution of the heating chamber is not uniform, the flue gas discharge regulating valve at a higher temperature is controlled to increase the opening, or the flue gas discharge regulating valve at a lower temperature is controlled to decrease the opening, thereby Adjust the temperature distribution of the heating chamber to make the temperature distribution in the heating chamber uniform

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小时左右即可完成,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 about 24 hours, which greatly improves work efficiency.

Claims (6)

1. a biomass pyrolytic charing equipment, it is characterized in that by body of heater, cover plate and be set up in pot in above furnace interior and form, described body of heater is provided with fume emission mouth, described cover plate for sealing is fastened on body of heater, cover plate and body of heater form heating chamber, cover plate and interior pot are formed and carbonize chamber, and the position that described cover plate corresponds to above interior pot is provided with the moisture exhausting mouth that can open and close; Form charring furnace burner hearth between described face, the interior the bottom of a pan and the diapire of heating chamber, in described burner hearth, be placed with burner; Described charing chamber and one extend to the pyrolysis gas expanding channels of body of heater outside.
2. biomass pyrolytic charing equipment according to claim 1, it is characterized in that described fume emission mouth has multiple, and be uniformly distributed in the sidewall of body of heater, described body of heater is provided with several temperature sensors, to detect the profiling temperatures of heating chamber; Described each fume emission mouth is equipped with the fume emission variable valve for changing fume emission mouth aperture; Described temperature sensor, fume emission variable valve are all electrically connected with a control unit, and described control unit controls the aperture of fume emission variable valve according to the information of temperature sensor.
3. biomass pyrolytic charing equipment according to claim 2, it is characterized in that described fume emission mouth is connected with a flue gas exhausting pipe line, described flue gas exhausting pipe line is provided with vacuum fan, and described vacuum fan is electrically connected with control unit.
4. the biomass pyrolytic charing equipment according to claim 1 or 2 or 3, is characterized in that described pyrolysis gas passage is provided with the valve be electrically connected with control unit.
5. the biomass pyrolytic charing equipment according to claim 1 or 2 or 3, is characterized in that being provided with several thermopairs in described charing chamber, to detect the profiling temperatures in charing chamber.
6. the biomass pyrolytic charing equipment according to claim 1 or 2 or 3, is characterized in that being placed with several open-topped iron cage frames in described charing chamber, and leaves gap between adjacent iron cage frame.
CN201520432444.2U 2015-06-23 2015-06-23 A biomass pyrolysis carbonization equipment Withdrawn - After Issue CN204897824U (en)

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Application Number Priority Date Filing Date Title
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