CN103700302B - A kind of pyrolysis of waste integrated experimental device for education experiment - Google Patents
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Abstract
Description
技术领域 technical field
本发明涉及用于废弃物热解资源化相关课程实验教学技术领域,尤其是涉及一种用于教学实验的废弃物热解一体化实验装置。 The invention relates to the technical field of experimental teaching for courses related to waste pyrolysis and resource utilization, in particular to an integrated waste pyrolysis experimental device used for teaching experiments.
背景技术 Background technique
环境科学与工程学科随着科学技术的进步与发展,其内涵和外延得到了不断的扩展,对培养高素质环境人才所必需的实验教学提出了更高的要求。为此,在保持传统实验教学优势和作用的同时,根据环境学科发展需要,积极探索建立与学科发展水平相一致的、适合于本科生实验的教学项目,使传统实验教学与学科发展需求有机结合,达到相互补充,实现最佳结合。 With the progress and development of science and technology, the connotation and extension of environmental science and engineering disciplines have been continuously expanded, which puts forward higher requirements for the experimental teaching necessary to cultivate high-quality environmental talents. To this end, while maintaining the advantages and functions of traditional experimental teaching, according to the development needs of environmental disciplines, actively explore and establish teaching projects that are consistent with the development level of the discipline and suitable for undergraduate experiments, so as to organically combine traditional experimental teaching with the development needs of the discipline. , to complement each other and achieve the best combination.
电子废弃物是一种新型废弃物,近年来,为世界上增长速度最快的固体废弃物,其增长速度是普通固体废弃物的3倍,它具有环境危害性和资源再生利用价值等特点,电子废弃物处理与资源化利用已成为当前研究的热点与重点。但目前,国内高校在本科生中仅开设以生活垃圾为主的固体废弃物实验,电子废弃物处理与资源化实验教学尚处于探索阶段,尤其以电子废弃物非金属粉末热解资源化的教学实验尚未见报道。本实验教学装置的成功研发,不仅体现着学科前沿发展与解决实际环境问题的特色,注重实验项目创新性以及实际应用意义,而且进一步完善了本科生固体废弃物实验内容,成为实验教学层次水平提升与创新的重要内容。该实验装置满足了本科学生实验需求,具有复套数强、操作简便、价格合理,实验教学效果好等特点。同时有效地解决了工程或科研用装置系统复杂、体积大,造价高,学生只能开展参观或演示实验的不足,提高了学生实验效果。 Electronic waste is a new type of waste. In recent years, it has become the fastest-growing solid waste in the world. Its growth rate is three times that of ordinary solid waste. It has the characteristics of environmental hazards and resource recycling value. The treatment and resource utilization of electronic waste has become the focus and focus of current research. However, at present, domestic colleges and universities only offer solid waste experiments mainly for domestic garbage among undergraduates, and the teaching of e-waste treatment and recycling experiments is still in the exploratory stage, especially the teaching of e-waste non-metallic powder pyrolysis and recycling. Experiments have not been reported yet. The successful research and development of this experimental teaching device not only embodies the characteristics of the frontier development of the subject and solving practical environmental problems, but also pays attention to the innovation of experimental projects and the significance of practical application, and further improves the experimental content of solid waste for undergraduates, becoming an improvement in the level of experimental teaching. Important content with innovation. The experimental device meets the experimental needs of undergraduate students, and has the characteristics of strong multiple sets, easy operation, reasonable price, and good experimental teaching effect. At the same time, it effectively solves the problem that the engineering or scientific research device system is complex, large in size and high in cost, and students can only conduct visits or demonstration experiments, and improves the experimental effect of students.
发明内容 Contents of the invention
为了解决上述问题,本发明提供一种教学用废弃物热解一体化实验装置,可适用于电子废弃物及其他有机高分子物料热解实验,实验装置结构简单、操作方便,易于拆卸、密封性能好,能满足环境、化工等相关专业的大学生实验教学需求。 In order to solve the above problems, the present invention provides an integrated experimental device for pyrolysis of waste for teaching, which is suitable for pyrolysis experiments of electronic waste and other organic polymer materials. The experimental device has simple structure, convenient operation, easy disassembly, and good sealing performance. Good, it can meet the experimental teaching needs of college students majoring in environment, chemical engineering and other related majors.
为了达到上述目的,本发明的解决方案是: In order to achieve the above object, the solution of the present invention is:
本发明提出的一种用于教学实验的废弃物热解一体化实验装置,由料槽2、热解反应器3、弯头5、气液收集器6、冷凝器7、气液输送管8、气液分离器9、接油杯10和废气排气管11组成,其特征在于:热解反应器3水平放置,冷凝器7垂直放置,热解反应器3内设有热电偶,热解反应器3一端连接进气管1,另一端与弯头5相连,热解反应器3内部中央设置加料用料槽2,弯头5与冷凝器7上端相连,冷凝器7上端内部设置圆弧形气液收集器6,冷凝器7内设有斜管8,斜管8与水平面倾斜角度为75-80°,气液收集器6的出口对准斜管8,气液分离器9呈倒圆台形,位于冷凝器7下方,气液分离器9另一端连接接油杯10。 A waste pyrolysis integrated experimental device for teaching experiments proposed by the present invention consists of a material tank 2, a pyrolysis reactor 3, an elbow 5, a gas-liquid collector 6, a condenser 7, and a gas-liquid delivery pipe 8 , a gas-liquid separator 9, an oil cup 10 and an exhaust gas exhaust pipe 11, characterized in that: the pyrolysis reactor 3 is placed horizontally, the condenser 7 is placed vertically, and the pyrolysis reactor 3 is provided with a thermocouple, and the pyrolysis One end of the reactor 3 is connected to the inlet pipe 1, and the other end is connected to the elbow 5. The feed tank 2 is arranged in the center of the pyrolysis reactor 3, and the elbow 5 is connected to the upper end of the condenser 7. The upper end of the condenser 7 is provided with an arc-shaped The gas-liquid collector 6 and the condenser 7 are provided with an inclined tube 8, the angle of inclination between the inclined tube 8 and the horizontal plane is 75-80°, the outlet of the gas-liquid collector 6 is aligned with the inclined tube 8, and the gas-liquid separator 9 is rounded Bench-shaped, located below the condenser 7, the other end of the gas-liquid separator 9 is connected to the oil receiving cup 10.
本发明中,热解反应器3与弯头5通过密封圈和快开卡套连接,弯头5与冷凝器7通过密封圈和快开卡套连接;气液分离器9与接油杯10通过密封圈和快开卡套连接。 In the present invention, the pyrolysis reactor 3 is connected to the elbow 5 through a sealing ring and a quick-open ferrule, and the elbow 5 is connected to the condenser 7 through a seal ring and a quick-open ferrule; the gas-liquid separator 9 is connected to the oil receiving cup 10 It is connected by a sealing ring and a quick release ferrule.
本发明中,所述斜管8为热解气液输送管,若干根斜管8平行布置,均匀分布于冷凝器7内,斜管8根数为2-5根,。 In the present invention, the inclined pipes 8 are pyrolysis gas-liquid delivery pipes, several inclined pipes 8 are arranged in parallel and evenly distributed in the condenser 7, and the number of eight inclined pipes is 2-5.
本发明中,所述冷凝器7内设置有一热解废气排放管11,其一端与气液分离器9相连,另一端通过冷凝器内壁引出并经2组酸性液体吸收装置吸收后排放。 In the present invention, the condenser 7 is provided with a pyrolysis waste gas discharge pipe 11, one end of which is connected to the gas-liquid separator 9, and the other end is led out through the inner wall of the condenser and discharged after being absorbed by two sets of acid liquid absorption devices.
本发明中,冷凝器7内冷凝水通过泵循环。 In the present invention, the condensed water in the condenser 7 is circulated by a pump.
本发明中,所述装置使用时,将热解反应器3放置于加热装置13内,进气管1与氮气瓶相连,加热装置13与温度程序控制器12相连。 In the present invention, when the device is in use, the pyrolysis reactor 3 is placed in the heating device 13 , the gas inlet pipe 1 is connected to the nitrogen cylinder, and the heating device 13 is connected to the temperature program controller 12 .
本发明中,所述加热装置内的加热元件采用硅碳棒,加热温度最高为1100℃,双层壳体结构,炉膛采用氧化铝多晶体纤维材料,具有温场均衡、表面温度低等特点。 In the present invention, the heating element in the heating device adopts silicon carbide rods, the heating temperature is up to 1100°C, the double-layer shell structure, and the furnace adopts alumina polycrystalline fiber material, which has the characteristics of balanced temperature field and low surface temperature.
本发明中,所述温度程序控制器12采用10段程序控温系统,移相触发、可控硅控制。 In the present invention, the temperature program controller 12 adopts a 10-segment program temperature control system, phase-shift trigger, and thyristor control.
由于采用了上述技术方案,本发明具有以下有益效果: Owing to adopting above-mentioned technical scheme, the present invention has following beneficial effect:
1、与通常的管式热解装置相比,本教学用热解一体化实验装置具有结构简单、拆卸方便、温场均匀、表面温度低、体积小等特点。热解反应器不仅增大了对物料的加热表面,而且与管壁加热形成协同效应,强化了传热效果,有效解决了由于加热不均匀带来的热解反应不完全和副产物较多的问题。 1. Compared with the usual tubular pyrolysis device, this integrated pyrolysis experimental device for teaching has the characteristics of simple structure, convenient disassembly, uniform temperature field, low surface temperature and small volume. The pyrolysis reactor not only increases the heating surface of the material, but also forms a synergistic effect with the heating of the tube wall, which strengthens the heat transfer effect and effectively solves the problem of incomplete pyrolysis reaction and many by-products caused by uneven heating. question.
2、热解反应器与垂直的冷凝器用相同管径的弯头相连接,并采用氟橡胶O型密封圈、卡通式快开卡套连接。对快开卡套按气体流向,在流出端增加止口,能有效阻止粘稠热解反应产物与接口部位的接触,有效防止热解产物在密封连接部位的凝固和淤积而导致上端盖不易开启的问题;此外,每个接口处均用卡通式快开卡套连接,易于每个部件拆卸、清洗。 2. The pyrolysis reactor and the vertical condenser are connected with an elbow of the same pipe diameter, and are connected by a fluorine rubber O-ring and a cartoon-style quick-open ferrule. According to the gas flow direction of the quick-opening ferrule, a stop is added at the outflow end, which can effectively prevent the viscous pyrolysis reaction product from contacting the interface part, and effectively prevent the pyrolysis product from solidifying and accumulating at the sealing connection part, which will cause the upper end cover to be difficult to open In addition, each interface is connected with a cartoon-style quick-release ferrule, which is easy to disassemble and clean each part.
3、冷凝器下端与储油杯采用卡通式快开接通连接,且冷凝器下端内壁采用倒圆台型结构,以保证液态热解油流入储油杯中(玻璃杯),不使热解油在接头处滞留粘结。 3. The lower end of the condenser and the oil storage cup are connected by a cartoon-type quick-open connection, and the inner wall of the lower end of the condenser adopts a rounded platform structure to ensure that the liquid pyrolysis oil flows into the oil storage cup (glass cup) without causing the pyrolysis oil to Adhesion stuck in joints.
附图说明 Description of drawings
图1是本发明教学用热解反应冷凝一体化装置的结构剖视图。 Fig. 1 is a structural cross-sectional view of an integrated device for pyrolysis reaction and condensation for teaching in the present invention.
图2是包含图1所示实施例的电子废弃物非金属粉末热解资源化反应装置示意图。 Fig. 2 is a schematic diagram of a pyrolysis recycling reaction device for non-metallic powder of electronic waste including the embodiment shown in Fig. 1 .
图中标号:1为进气管,2为料槽,3为热解反应器,4为快开卡套,5为弯头,6为气液收集器,7为冷凝器,8为斜管,9为气液分离器,10为接油杯,11为废气排放管,12为温度程序控制器,13为加热装置。 Numbers in the figure: 1 is the intake pipe, 2 is the trough, 3 is the pyrolysis reactor, 4 is the quick-open ferrule, 5 is the elbow, 6 is the gas-liquid collector, 7 is the condenser, 8 is the inclined pipe, 9 is a gas-liquid separator, 10 is an oil cup, 11 is a waste gas discharge pipe, 12 is a temperature program controller, and 13 is a heating device.
具体实施方式 Detailed ways
以下结合附图所示实施例对本发明作进一步的说明。 The present invention will be further described below in conjunction with the embodiments shown in the accompanying drawings.
实施例1:本发明提出的教学用热解反应冷凝一体化装置,由热解反应器3、料槽2、气液输送管8、冷凝器7、气液分离器9、接油杯10、弯头5、快开卡套4和废气排放管11等组成,结构如图1所示。热解反应器3内设有热电偶,进气管1与热解反应器3左端相连,右端通过快开卡套4与弯头5相连,采用氟橡胶垫片密封,保证其有很好的密封性。 Embodiment 1: The pyrolysis reaction condensation integrated device for teaching proposed by the present invention consists of a pyrolysis reactor 3, a hopper 2, a gas-liquid delivery pipe 8, a condenser 7, a gas-liquid separator 9, an oil receiving cup 10, Elbow 5, quick opening ferrule 4 and waste gas discharge pipe 11 etc. are composed, and the structure is as shown in Figure 1. There is a thermocouple inside the pyrolysis reactor 3, the inlet pipe 1 is connected to the left end of the pyrolysis reactor 3, and the right end is connected to the elbow 5 through the quick-open ferrule 4, and is sealed with a fluorine rubber gasket to ensure a good seal sex.
本发明中的测温热电偶置于热电偶套管内部,设置于热解反应器3侧壁,进气管1通过三通分别与载气输送管相连,为防止热解反应器3热解后的产物经弯头5后形成的气液产物集聚在冷凝器7上端,以免产生渗漏,特在冷凝器7上端设置了圆弧形气液收集器8。热解气随冷凝器7中3根Φ10mm气液输送管输送冷凝,形成液态油。为防止液态油在油杯上方集聚,特设置气液分离器9,并形成1150C倒角。热解废气随垂直的废气排气管11外排。 The temperature-measuring thermocouple in the present invention is placed inside the thermocouple casing, arranged on the side wall of the pyrolysis reactor 3, and the inlet pipe 1 is connected with the carrier gas delivery pipe respectively through a tee, so as to prevent the pyrolysis reactor 3 from pyrolyzing The gas-liquid product formed after the product passes through the elbow 5 gathers at the upper end of the condenser 7 to avoid leakage, and an arc-shaped gas-liquid collector 8 is specially arranged at the upper end of the condenser 7 . The pyrolysis gas is transported and condensed by three Φ10mm gas-liquid delivery pipes in the condenser 7 to form liquid oil. In order to prevent liquid oil from accumulating above the oil cup, a gas-liquid separator 9 is specially provided, and a 115°C chamfer is formed. The pyrolysis waste gas is discharged with the vertical waste gas exhaust pipe 11.
热解反应器3内设置加料用料槽2,热解反应器3左端与进气管1通过焊接方式相连,右端即热解产物排出端与弯头相连,弯头5与冷凝器7上端相连,并在冷凝器7上端内部设置圆弧形气液收集器6,收集的热解气体进入冷凝器7内3根平行的斜管,斜管倾斜角度控制在750左右,冷凝后的液体经气液分离器流入接油杯10,气液分离器9呈倒圆台形,冷凝后的热解废气沿Φ10mm垂直管上升后接入环境。每个连接处均设有快开卡套4,并采用氟橡胶垫片密封,保证整个装置的密封性能。 A feeding trough 2 is arranged in the pyrolysis reactor 3, the left end of the pyrolysis reactor 3 is connected to the inlet pipe 1 by welding, the right end is the discharge end of the pyrolysis product is connected to the elbow, and the elbow 5 is connected to the upper end of the condenser 7. An arc-shaped gas-liquid collector 6 is arranged inside the upper end of the condenser 7, and the collected pyrolysis gas enters three parallel inclined tubes in the condenser 7, and the inclination angle of the inclined tubes is controlled at about 75°, and the condensed liquid passes through the gas The liquid separator flows into the oil receiving cup 10, and the gas-liquid separator 9 is in the shape of a rounded frustum. The condensed pyrolysis waste gas rises along the Φ10mm vertical pipe and enters the environment. Each connection is provided with a quick-open ferrule 4, and is sealed with a fluororubber gasket to ensure the sealing performance of the entire device.
热解反应器3采用耐高温不锈钢SUS310S管,外径φ42,长40cm,水平放置。热解反应器内中央位置放置原料槽具,用于放置反应前热解原料及反应后热解残渣,一方面方便反应原料定位放置,另一方面使热解残渣与热解反应器管壁不易焦结,有利于残渣取出。热解反应器3一端密闭,开小孔2个,一个与外接载气相连,来推动热解反应器中反应气体朝反应产物出口端流动,在热解反应器3中部上方装有套管式热电偶,以正确测量热解反应器内反应温度;另一端经同管径弯头5与垂直冷凝器7相连接,并采用氟橡胶O型密封圈、卡通式快开卡套连接。对快开卡套按气体流向,在流出端增加止口,以方便操作及防止液态油残留。 The pyrolysis reactor 3 is made of high-temperature-resistant stainless steel SUS310S tube with an outer diameter of φ42 and a length of 40 cm, and is placed horizontally. The raw material tank is placed in the center of the pyrolysis reactor, which is used to place the pyrolysis raw materials before the reaction and the pyrolysis residue after the reaction. Coking is conducive to the removal of residues. One end of the pyrolysis reactor 3 is closed, with two small holes, one of which is connected to the external carrier gas to push the reaction gas in the pyrolysis reactor to flow toward the outlet of the reaction product. The thermocouple is used to correctly measure the reaction temperature in the pyrolysis reactor; the other end is connected to the vertical condenser 7 through the elbow 5 of the same pipe diameter, and is connected by a fluororubber O-ring and a cartoon-type quick-opening ferrule. According to the gas flow direction of the quick-open ferrule, a stop is added at the outflow end to facilitate operation and prevent liquid oil residue.
冷凝器7内设3根φ10mm斜管8,斜管8的倾角为75°,作为热解气液输送管,与冷凝器7平行且均匀分布,使一定温度的含油热解气迅速通过并冷凝成为热解油,在冷凝器7下端的快开卡套内壁采用倒圆台型,促使液态油落入接油杯10(玻璃杯)中,防止液态油在接口处残留。而冷凝水用泵At103循环,使之连续循环使用。 Three φ10mm inclined tubes 8 are installed in the condenser 7, and the inclined tubes 8 have an inclination angle of 75°, which are used as pyrolysis gas-liquid delivery pipes, parallel and evenly distributed with the condenser 7, so that the oil-containing pyrolysis gas at a certain temperature can quickly pass through and condense To become pyrolysis oil, the inner wall of the quick-open ferrule at the lower end of the condenser 7 adopts a rounded table shape to promote the liquid oil to fall into the oil receiving cup 10 (glass cup) to prevent the liquid oil from remaining at the interface. The condensed water is circulated by the pump At103 to make it continuously circulated.
热解废气排气及吸附系统,在冷凝器内设置一热解废气排放管φ10mm,与冷凝器平行,下端与气液分离器9相连,上端经弯头后通过冷凝器7侧壁引出并经2组酸性液体吸附装置吸附后排出,避免热解气对环境的影响。 Pyrolysis waste gas exhaust and adsorption system, a pyrolysis waste gas discharge pipe φ10mm is installed in the condenser, parallel to the condenser, the lower end is connected with the gas-liquid separator 9, and the upper end is led out through the side wall of the condenser 7 after passing through the elbow and passed through 2 groups of acidic liquid adsorption devices are adsorbed and then discharged to avoid the impact of pyrolysis gas on the environment.
如图2所示,为采用本发明教学用热解反应一体化实验装置的工作原理示意图,本发明位于加热装置13中,进气管1与氮气瓶相连。 As shown in Fig. 2, it is a schematic diagram of the working principle of the pyrolysis reaction integrated experimental device for teaching of the present invention. The present invention is located in the heating device 13, and the inlet pipe 1 is connected to the nitrogen cylinder.
加热装置13,其加热元件采用硅碳棒,加热温度最高为1100℃,双层壳体结构,炉膛采用氧化铝多晶体纤维材料,具有温场均衡、表面温度低、炉体体积小等特点。 The heating device 13 uses silicon carbide rods as its heating element, and the maximum heating temperature is 1100°C. It has a double-layer shell structure, and the furnace is made of alumina polycrystalline fiber material. It has the characteristics of balanced temperature field, low surface temperature, and small furnace volume.
温度程序控制器12,对热解反应器3所需的目标温度设置升温速率,采用10段程序控温系统,移相触发、可控硅控制,实现可调的升温程序。 The temperature program controller 12 sets the temperature rise rate for the target temperature required by the pyrolysis reactor 3, adopts a 10-stage program temperature control system, phase-shift trigger, and thyristor control to realize an adjustable temperature rise program.
为了验证发明的实验装置的产油情况,具体情况如下: In order to verify the oil production situation of the experimental device invented, the specific circumstances are as follows:
(1)用香蕉水对实验装置反应器3内壁、弯头5、设置于冷凝器内的气液收集器6、气液输送器8、气液分离器9、废气排气管11及接油杯10进行冲洗,去除残留物质; (1) Use banana water to treat the inner wall of the experimental device reactor 3, the elbow 5, the gas-liquid collector 6 installed in the condenser, the gas-liquid conveyor 8, the gas-liquid separator 9, the exhaust gas exhaust pipe 11 and the oil connection Cup 10 is rinsed to remove residual substances;
(2)称取非金属细颗粒料m=49g; (2) Weigh non-metal fine particle material m=49g;
(3)实验参数:载气--氩气,气流--1L/min,程序升温--8.94℃/min,保温温度--500℃(保温30min); (3) Experimental parameters: carrier gas - argon, air flow - 1L/min, programmed temperature rise - 8.94°C/min, holding temperature - 500°C (holding time 30min);
(4)实验结束,取出煅烧后残留固体称重为36.2636g,计算理论产油量(有部分热解气)为12.7364g,理论产油率为25.99%; (4) At the end of the experiment, take out the residual solid after calcination and weigh 36.2636g, calculate the theoretical oil production (with some pyrolysis gas) as 12.7364g, and the theoretical oil production rate is 25.99%;
(5)通过多次实验验证,在物料50g,保温500℃,30min时实验效果较好。 (5) It has been verified through multiple experiments that the experimental effect is better when the material is 50g and the temperature is kept at 500°C for 30 minutes.
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