CN207619331U - A kind of comprehensive resources regeneration Poly-generation cycle furnace apparatus - Google Patents
A kind of comprehensive resources regeneration Poly-generation cycle furnace apparatus Download PDFInfo
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- CN207619331U CN207619331U CN201721462809.1U CN201721462809U CN207619331U CN 207619331 U CN207619331 U CN 207619331U CN 201721462809 U CN201721462809 U CN 201721462809U CN 207619331 U CN207619331 U CN 207619331U
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- 230000008929 regeneration Effects 0.000 title claims abstract description 10
- 238000011069 regeneration method Methods 0.000 title claims abstract description 10
- 230000005540 biological transmission Effects 0.000 claims abstract description 19
- 229920000742 Cotton Polymers 0.000 claims description 4
- 238000004321 preservation Methods 0.000 claims 1
- 239000002699 waste material Substances 0.000 abstract description 16
- 238000000197 pyrolysis Methods 0.000 abstract description 9
- 238000007599 discharging Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 13
- 239000002028 Biomass Substances 0.000 description 5
- 239000003921 oil Substances 0.000 description 5
- 241000283690 Bos taurus Species 0.000 description 4
- 239000003610 charcoal Substances 0.000 description 4
- 210000003608 fece Anatomy 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 239000010813 municipal solid waste Substances 0.000 description 4
- 239000010802 sludge Substances 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000009413 insulation Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 241000282414 Homo sapiens Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003034 coal gas Substances 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 230000002459 sustained effect Effects 0.000 description 1
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Abstract
一种综合资源再生多联产循环炉装置,包括炉体(1)、PLC控制器和驱动装置(2),炉体(1)内部设置有刮板链条装置(6),炉体(1)两端分别设置有主动传动装置(8)和从动传动装置(9),刮板链条装置(6)包括链条,链条上设置有多个刮板,链条分别与主动传动装置(8)和从动传动装置(9)相连接,主动传动装置(8)与驱动装置(2)相连接,导热管(5)上设置有温度传感器,温度传感器与PLC控制器相连接,驱动装置(2)与PLC控制器相连接。刮板链条装置(6)移动带废弃物移动加热,通过控制刮板链条装置(6)移动速度及出料、进料时间,从而使得废弃物停留热解时间可以控制。
A comprehensive resource regeneration multi-generation cycle furnace device, including a furnace body (1), a PLC controller and a driving device (2), the furnace body (1) is equipped with a scraper chain device (6), and the furnace body (1) The two ends are respectively provided with a driving transmission device (8) and a driven transmission device (9). The scraper chain device (6) includes a chain on which a plurality of scrapers are arranged. The chain is respectively connected with the driving transmission device (8) and the slave The active transmission device (9) is connected, the active transmission device (8) is connected with the driving device (2), the heat pipe (5) is provided with a temperature sensor, the temperature sensor is connected with the PLC controller, the driving device (2) is connected with the PLC controller is connected. The moving belt of the scraper chain device (6) moves and heats the waste, and by controlling the moving speed of the scraper chain device (6) and the time of discharging and feeding, the residence time of the waste in pyrolysis can be controlled.
Description
技术领域technical field
本实用新型涉及一种设备,更具体的说涉及一种综合资源再生多联产循环炉装置,属于资源循环再利用技术领域。The utility model relates to equipment, more specifically to a comprehensive resource regeneration polygeneration cycle furnace device, which belongs to the technical field of resource recycling.
背景技术Background technique
生物质能是仅次于石油、煤炭和天然气的世界第4大能源,具有可再生和环境友好的双重属性,占世界可再生能源消费量78%;生物质能的发展和应用对社会经济可持续发展具有重要意义。同时,牛粪、城市生活垃圾、污泥等多种废弃物如不加以循环利用,则对人类生活环境产生较大影响;因此,对生物质及牛粪、城市生活垃圾、污泥等多种废弃物综合循环利用的废弃物联产装置应运而生。Biomass energy is the fourth largest energy source in the world after oil, coal and natural gas. It is renewable and environmentally friendly, accounting for 78% of the world's renewable energy consumption. Sustained development is of great significance. At the same time, if various wastes such as cow dung, municipal solid waste, and sludge are not recycled, they will have a great impact on the living environment of human beings; A waste cogeneration device for comprehensive recycling of waste came into being.
目前,现有的废弃物联产装置中,废弃物根据自身重量在炉体内下降同时进行热解。但是,该装置中加热温度一般为450左右,且无法控制废弃物热解时间和速度;因此存在产物品质不高、能源转换与利用率低、燃料成型电耗高等问题。At present, in the existing waste cogeneration device, the waste is pyrolyzed while falling in the furnace body according to its own weight. However, the heating temperature in this device is generally around 450, and the time and speed of waste pyrolysis cannot be controlled; therefore, there are problems such as low product quality, low energy conversion and utilization rate, and high power consumption for fuel forming.
发明内容Contents of the invention
本实用新型的目的在于针对现有的废弃物联产装置存在的温度较低、无法控制热解时间和速度等问题,提供一种综合资源再生多联产循环炉装置。The purpose of the utility model is to provide a comprehensive resource regeneration multi-generation circulating furnace device for the problems of low temperature and uncontrollable pyrolysis time and speed in the existing waste cogeneration device.
本实用新型为实现上述目的,所采用技术解决方案是:一种综合资源再生多联产循环炉装置,包括炉体、PLC控制器和驱动装置,所述的炉体顶部设置有进料口,炉体上设置有出气口,炉体内部上方布置有导热管,炉体一端设置有卸料口,且炉体内部设置有刮板链条装置,炉体两端分别设置有主动传动装置和从动传动装置,所述的刮板链条装置包括链条,所述的链条上设置有多个刮板,链条分别与主动传动装置和从动传动装置相连接,所述的主动传动装置与驱动装置相连接,所述的导热管上设置有温度传感器,所述的温度传感器与PLC控制器相连接,所述的驱动装置与PLC控制器相连接。In order to achieve the above purpose, the utility model adopts a technical solution as follows: a comprehensive resource regeneration multi-generation circulating furnace device, including a furnace body, a PLC controller and a driving device. The top of the furnace body is provided with a feeding port, There is a gas outlet on the furnace body, a heat conduction pipe is arranged above the inside of the furnace body, a discharge port is arranged at one end of the furnace body, and a scraper chain device is installed inside the furnace body, and an active transmission device and a driven drive device are respectively installed at both ends of the furnace body. Transmission device, the scraper chain device includes a chain, the chain is provided with a plurality of scrapers, the chains are respectively connected with the driving device and the driven transmission device, and the driving device is connected with the driving device , the heat pipe is provided with a temperature sensor, the temperature sensor is connected to the PLC controller, and the driving device is connected to the PLC controller.
所述的炉体内部导热管上方布置有保温棉。Insulation cotton is arranged above the heat pipe inside the furnace body.
所述的出气口与导热管相连通。The air outlet communicates with the heat pipe.
所述的炉体底部设置有支架。The bottom of the furnace body is provided with a bracket.
与现有技术相比较,本实用新型的有益效果是:Compared with the prior art, the beneficial effects of the utility model are:
1、本实用新型中刮板链条装置移动带废弃物移动加热,通过控制刮板链条装置移动速度及出料、进料时间,从而使得废弃物停留热解时间可以控制。1. In the utility model, the moving belt of the scraper chain device moves and heats the waste, and by controlling the moving speed of the scraper chain device and the time of discharging and feeding, the time for the waste to stay in pyrolysis can be controlled.
2、本实用新型中出气口与导热管相连通,使得本装置产生的气体可以给自己提供热力能源;加热温度为300-700度且自控调节。2. In the utility model, the air outlet is connected with the heat pipe, so that the gas generated by the device can provide thermal energy for itself; the heating temperature is 300-700 degrees and is automatically controlled and adjusted.
附图说明Description of drawings
图1是本实用新型结构示意图。Fig. 1 is the structural representation of the utility model.
图2是本实用新型俯视图。Fig. 2 is a top view of the utility model.
图中,炉体1,驱动装置2,进料口3,出气口4,导热管5,刮板链条装置6,保温棉7,主动传动装置8,从动传动装置9,支架10。Among the figure, furnace body 1, driving device 2, feed inlet 3, air outlet 4, heat pipe 5, scraper chain device 6, heat insulating cotton 7, driving transmission device 8, driven transmission device 9, support 10.
具体实施方式Detailed ways
以下结合附图说明和具体实施方式对本实用新型作进一步的详细描述。The utility model will be described in further detail below in conjunction with the accompanying drawings and specific embodiments.
参见图1至图2,一种综合资源再生多联产循环炉装置,包括炉体1、PLC控制器和驱动装置2。所述的炉体1顶部设置有进料口3,炉体上设置有出气口4,炉体1内部上方布置有导热管5,炉体1一端设置有卸料口;且炉体1内部设置有刮板链条装置6,炉体1两端分别设置有主动传动装置8和从动传动装置9。所述的刮板链条装置6包括链条,所述的链条上设置有多个刮板,链条分别与主动传动装置8和从动传动装置9相连接;所述的主动传动装置8与驱动装置2相连接。所述的导热管5上设置有温度传感器,所述的温度传感器与PLC控制器相连接,所述的驱动装置2与PLC控制器相连接。导热管5上的温度通过温度传感器传给PLC控制器, PLC控制器控制驱动装置2;驱动装置2控制主动传动装置8通过刮板链条装置6移动带废弃物移动加热,进而控制刮板链条装置6移动速度及出料、进料时间,从而使得废弃物停留热解时间可以控制。Referring to Fig. 1 to Fig. 2, a comprehensive resource regeneration polygeneration cycle furnace device includes a furnace body 1, a PLC controller and a driving device 2. The top of the furnace body 1 is provided with a feed inlet 3, the furnace body is provided with an air outlet 4, a heat pipe 5 is arranged above the inside of the furnace body 1, and a discharge port is provided at one end of the furnace body 1; and the furnace body 1 is provided with a There is a scraper chain device 6, and the two ends of the furnace body 1 are respectively provided with a driving transmission device 8 and a driven transmission device 9. Described scraper chain device 6 comprises a chain, and described chain is provided with a plurality of scrapers, and chain is connected with driving transmission device 8 and driven transmission device 9 respectively; Described driving transmission device 8 and driving device 2 connected. The heat pipe 5 is provided with a temperature sensor, the temperature sensor is connected to the PLC controller, and the driving device 2 is connected to the PLC controller. The temperature on the heat pipe 5 is transmitted to the PLC controller through the temperature sensor, and the PLC controller controls the driving device 2; the driving device 2 controls the active transmission device 8 to move and heat the waste through the scraper chain device 6, and then controls the scraper chain device 6 The moving speed and the time of discharging and feeding, so that the time of waste pyrolysis can be controlled.
参见图1至图2,所述的炉体1内部导热管5上方布置有保温棉7。Referring to Fig. 1 to Fig. 2 , thermal insulation cotton 7 is arranged above the heat pipe 5 inside the furnace body 1 .
参见图1至图2,所述的出气口4与导热管5相连通。使得本装置产生的气体可以给自己提供热力能源。Referring to FIG. 1 to FIG. 2 , the air outlet 4 communicates with the heat pipe 5 . The gas generated by the device can provide thermal energy for itself.
参见图1至图2,所述的炉体1底部设置有支架10。支架10通常由用户确定高度并现场制作安装。Referring to FIG. 1 to FIG. 2 , a bracket 10 is provided at the bottom of the furnace body 1 . The height of the bracket 10 is usually determined by the user and fabricated and installed on site.
参见图1至图2,物料通过进料口3进料,刮板链条装置6带动物料运行,温度传感器上的温度传到PLC控制器,PLC控制器控制驱动装置2,进而实现热解速度快慢自动可调。炉体1内部通过导热管5加热,炉体1产生的气体通过出气口4进入导热管5,据统计约有68%炉体1产生的气体供给导热管5加热,加热温度为300-700度且自控调节。Referring to Figure 1 to Figure 2, the material is fed through the feed port 3, the scraper chain device 6 drives the material to run, the temperature on the temperature sensor is transmitted to the PLC controller, and the PLC controller controls the driving device 2, thereby realizing the speed of pyrolysis Automatically adjustable. The inside of the furnace body 1 is heated by the heat conduction tube 5, and the gas generated by the furnace body 1 enters the heat conduction tube 5 through the gas outlet 4. According to statistics, about 68% of the gas generated by the furnace body 1 is supplied to the heat conduction tube 5 for heating, and the heating temperature is 300-700 degrees And self-control adjustment.
参见图1至图2,使用本装置处理牛粪、生物质、城市生活垃圾、污泥等,将废弃物通过炉体热解后吃干榨净产生炭、气、油产品。在热解温度为600-700度时热解产生的炭类(牛粪炭、生物质炭、城市垃圾无机物、污泥等)均4000-7000大卡、可燃烧燃气(生物质燃气、牛粪气、垃圾气等)均2300-3800大卡、燃烧油(生物质油、垃圾油燃烧)均7000-8000大卡。导热管5加热消耗炉体1产生的约68%燃气可以维持平衡;同时炉内1箱体全密封,燃气压力控制-500至500千帕左右,炉内1温度可以达到600-900度,能够对废弃物进行无氧热解。Referring to Figures 1 to 2, this device is used to treat cow dung, biomass, municipal solid waste, sludge, etc., and the waste is pyrolyzed through the furnace body, eaten dry and squeezed to produce charcoal, gas, and oil products. When the pyrolysis temperature is 600-700 degrees, the charcoal produced by pyrolysis (cow dung charcoal, biomass charcoal, urban waste inorganic matter, sludge, etc.) has an average of 4000-7000 kcal, and the combustible gas (biomass gas, cattle Dung gas, garbage gas, etc.) are 2300-3800 kcal, and combustion oil (biomass oil, garbage oil combustion) is 7000-8000 kcal. The heat pipe 5 heats and consumes about 68% of the gas produced by the furnace body 1 to maintain a balance; at the same time, the furnace body 1 is fully sealed, the gas pressure is controlled at about -500 to 500 kPa, and the temperature of the furnace body 1 can reach 600-900 degrees, which can Anaerobic pyrolysis of waste.
以上内容是结合具体的优选实施方式对本实用新型所作的进一步详细说明,不能认定本实用新型的具体实施只局限于这些说明。对于本实用新型所属技术领域的普通技术人员来说,在不脱离本实用新型构思的前提下,还可以做出若干简单推演或替换,上述结构都应当视为属于本实用新型的保护范围。The above content is a further detailed description of the utility model in combination with specific preferred embodiments, and it cannot be assumed that the specific implementation of the utility model is only limited to these descriptions. For those of ordinary skill in the technical field to which the utility model belongs, some simple deduction or replacement can also be made without departing from the concept of the utility model, and the above structures should be regarded as belonging to the protection scope of the utility model.
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