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CN111676039A - A biomass pyrolysis carbonization system - Google Patents

A biomass pyrolysis carbonization system Download PDF

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Publication number
CN111676039A
CN111676039A CN202010716518.0A CN202010716518A CN111676039A CN 111676039 A CN111676039 A CN 111676039A CN 202010716518 A CN202010716518 A CN 202010716518A CN 111676039 A CN111676039 A CN 111676039A
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pyrolysis
furnace body
purification
carbonization system
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王宏燕
郑函
马晓伟
李传宝
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Northeast Agricultural University
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C10B53/02Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of cellulose-containing material
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B47/00Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
    • C10B47/28Other processes
    • C10B47/30Other processes in rotary ovens or retorts
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B57/00Other carbonising or coking processes; Features of destructive distillation processes in general
    • 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

本发明公开一种生物质热解炭化系统,包括依次相连的进料仓、炉体、粉尘分离器、净化沉降装置、冷凝塔、热解气回收利用装置和热解液收集装置,进料仓与炉体的入口相连通,炉体具有加热元件,加热元件能够对炉体内的物料进行加热,物料由进料仓加入,继而进入炉体中,炉体旋转并加热物料,物料热解,粉尘分离器能够分离热解过程中的产物和原料粉尘,热解产生的蒸汽进入净化沉降装置中,净化沉降装置能够对热解蒸汽进行净化与沉降,净化后的热解蒸汽进入冷凝塔中,冷凝塔冷却热解蒸汽,分离热解气和热解液,热解气回收利用装置能够收集分离出的热解气,热解液进入热解液收集装置,电控单元能够控制炉体的转速并监测炉体内热解温度。

Figure 202010716518

The invention discloses a biomass pyrolysis and carbonization system, comprising a feed bin, a furnace body, a dust separator, a purification settling device, a condensation tower, a pyrolysis gas recovery and utilization device, and a pyrolysis liquid collection device, which are connected in sequence. It is connected with the inlet of the furnace body. The furnace body has a heating element. The heating element can heat the material in the furnace body. The material is added from the feed bin and then enters the furnace body. The furnace body rotates and heats the material. The material is pyrolyzed and dust The separator can separate the products and raw material dust in the pyrolysis process. The steam generated by the pyrolysis enters the purification and sedimentation device. The purification and sedimentation device can purify and settle the pyrolysis steam. The purified pyrolysis steam enters the condensing tower and condenses. The tower cools the pyrolysis steam, separates the pyrolysis gas and the pyrolysis liquid. The pyrolysis gas recovery and utilization device can collect the separated pyrolysis gas, and the pyrolysis liquid enters the pyrolysis liquid collection device. The electric control unit can control the speed of the furnace body and Monitor the pyrolysis temperature in the furnace.

Figure 202010716518

Description

一种生物质热解炭化系统A biomass pyrolysis carbonization system

技术领域technical field

本发明涉及生物质热解炭化技术领域,特别是涉及一种生物质热解炭化系统。The invention relates to the technical field of biomass pyrolysis carbonization, in particular to a biomass pyrolysis carbonization system.

背景技术Background technique

生物质是指利用大气、水、土地等通过光合作用而产生的各种有机体,即一切有生命的可以生长的有机物质通称为生物质。生物质燃料是指将生物质材料燃烧作为燃料,一般主要是农林废弃物(如秸秆、锯末、甘蔗渣、稻糠等),主要区别于化石燃料。Biomass refers to various organisms produced by photosynthesis using the atmosphere, water, land, etc., that is, all living and growing organic substances are generally called biomass. Biomass fuel refers to the burning of biomass materials as fuel, generally mainly agricultural and forestry wastes (such as straw, sawdust, bagasse, rice bran, etc.), which are mainly different from fossil fuels.

随着社会的发展,生物质能源逐渐成为能源利用领域关注的热点。生物质热解炭化技术是生物质能源开发与利用的一种重要途径,其中热解炭化反应设备是核心装置,如何设计一种生物质炭化反应设备对生物质资源热解利用具有重要意义。目前常见的有两种类型的炭化设备,即窑式炭化炉和固定床式热解炉。窑式炭化炉包括传统窑式炭化炉和日本BA-I型炭化窑,其具有生产不连续,无法回收热解副产物的缺点。而浙江大学回转窑和三段式生物质热解窑虽然可以克服窑式炭化炉的缺点,但不能精确测定固定床式热解炉的热解参数,对固定床式热解炉的放大及中试工艺参数指导作用较小。With the development of society, biomass energy has gradually become a hot spot in the field of energy utilization. Biomass pyrolysis carbonization technology is an important way to develop and utilize biomass energy, in which the pyrolysis carbonization reaction equipment is the core device. How to design a biomass carbonization reaction equipment is of great significance for the pyrolysis and utilization of biomass resources. At present, there are two common types of carbonization equipment, namely kiln type carbonization furnace and fixed bed type pyrolysis furnace. Kiln-type carbonization furnaces include traditional kiln-type carbonization furnaces and Japanese BA-I type carbonization kilns, which have the disadvantages of discontinuous production and inability to recover pyrolysis by-products. While Zhejiang University rotary kiln and three-stage biomass pyrolysis kiln can overcome the shortcomings of kiln-type carbonization furnaces, they cannot accurately measure the pyrolysis parameters of fixed-bed pyrolysis furnaces. The parameter guidance effect is small.

因此,如何改变现有技术中,生物质热解炭化设备无法实现连续生产以及热解参数监测导致生产效率较低的现状,成为了本领域技术人员亟待解决的问题。Therefore, how to change the current situation that biomass pyrolysis carbonization equipment cannot achieve continuous production and low production efficiency due to pyrolysis parameter monitoring in the prior art has become an urgent problem for those skilled in the art.

发明内容SUMMARY OF THE INVENTION

本发明的目的是提供一种生物质热解炭化系统,以解决上述现有技术存在的问题,提高生物质热解炭化工作效率,降低操作人员劳动强度。The purpose of the present invention is to provide a biomass pyrolysis carbonization system, so as to solve the above problems existing in the prior art, improve the biomass pyrolysis carbonization work efficiency, and reduce the labor intensity of operators.

为实现上述目的,本发明提供了如下方案:本发明提供一种生物质热解炭化系统,包括依次相连的进料仓、炉体、粉尘分离器、净化沉降装置、冷凝塔、热解气回收利用装置和热解液收集装置,所述进料仓设置进料口,所述进料仓与所述炉体的入口相连通,所述炉体具有加热元件,所述加热元件能够对所述炉体内的物料进行加热,所述炉体的出口与所述粉尘分离器的入口相连通,所述炉体可转动地与所述粉尘分离器相连,所述粉尘分离器的出口与所述净化沉降装置的入口相连通,所述净化沉降装置的气体出口与所述冷凝塔的入口相连通,所述冷凝塔的气体出口与所述热解气回收利用装置的入口相连通,所述净化沉降装置的液体出口、所述冷凝塔的液体出口、所述热解气回收利用装置的液体出口均与所述热解液收集装置相连通;所述炉体还连接有电控单元,所述电控单元能够控制所述炉体的转速并监测所述炉体内的温度。In order to achieve the above purpose, the present invention provides the following solutions: The present invention provides a biomass pyrolysis carbonization system, including a feed bin, a furnace body, a dust separator, a purification settling device, a condensation tower, and a pyrolysis gas recovery that are connected in sequence. Using the device and the pyrolysis liquid collection device, the feed bin is provided with a feed port, the feed bin is communicated with the inlet of the furnace body, and the furnace body has a heating element, and the heating element can The material in the furnace body is heated, the outlet of the furnace body is communicated with the inlet of the dust separator, the furnace body is rotatably connected to the dust separator, and the outlet of the dust separator is connected to the dust separator. The inlet of the sedimentation device is connected, the gas outlet of the purification sedimentation device is connected with the inlet of the condensation tower, the gas outlet of the condensation tower is connected with the inlet of the pyrolysis gas recovery and utilization device, and the purification sedimentation device is connected. The liquid outlet of the device, the liquid outlet of the condensation tower, and the liquid outlet of the pyrolysis gas recovery and utilization device are all connected with the pyrolysis liquid collection device; the furnace body is also connected with an electric control unit, and the electric The control unit can control the rotational speed of the furnace body and monitor the temperature in the furnace body.

优选地,所述炉体包括外壳和内胆,所述内胆可转动地设置于所述外壳内,所述加热元件能够加热所述内胆内的物料,所述内胆内设置温度传感器,所述温度传感器与所述电控单元信号相连。Preferably, the furnace body includes an outer shell and an inner container, the inner container is rotatably arranged in the outer shell, the heating element can heat the material in the inner container, and a temperature sensor is arranged in the inner container, The temperature sensor is signal-connected to the electronic control unit.

优选地,所述内胆的内壁上设置旋转片,所述旋转片倾斜设置。Preferably, a rotating sheet is arranged on the inner wall of the inner pot, and the rotating sheet is arranged obliquely.

优选地,所述旋转片为四边形板状结构。Preferably, the rotating piece is a quadrilateral plate-like structure.

优选地,所述旋转片的数量为若干组,每组所述旋转片的数量为多片,多片所述旋转片绕所述内胆的轴线周状均布,若干组所述旋转片沿所述内胆的轴线等间距均布。Preferably, the number of the rotating pieces is several groups, and the number of the rotating pieces in each group is multiple pieces, the multiple pieces of the rotating pieces are evenly distributed around the axis of the inner tank, and the several groups of the rotating pieces are along the circumference of the inner tank. The axes of the inner pots are evenly spaced.

优选地,所述旋转片的数量为三组,每组所述旋转片的数量为四片。Preferably, the number of the rotating plates is three groups, and the number of the rotating plates in each group is four.

优选地,所述净化沉降装置的数量、所述冷凝塔的数量均为两组,两组所述净化沉降装置串联设置,两组所述冷凝塔串联设置。Preferably, the number of the purification settling devices and the number of the condensing towers are both two sets, the two sets of the purification settling devices are arranged in series, and the two sets of the condensation towers are arranged in series.

优选地,所述净化沉降装置的气体出口位于净化沉降装置的顶部,所述冷凝塔的气体出口位于所述冷凝塔的顶部,所述净化沉降装置的液体出口位于所述净化沉降装置的底部,所述冷凝塔的液体出口位于所述冷凝塔的底部。Preferably, the gas outlet of the purification settling device is located at the top of the purification settling device, the gas outlet of the condensation tower is located at the top of the condensation tower, and the liquid outlet of the purification settling device is located at the bottom of the purification settling device, The liquid outlet of the condensation tower is located at the bottom of the condensation tower.

优选地,所述加热元件采用燃气加热方式,所述热解气回收利用装置与所述加热元件相连通。Preferably, the heating element adopts a gas heating method, and the pyrolysis gas recovery and utilization device is communicated with the heating element.

本发明相对于现有技术取得了以下技术效果:本发明的生物质热解炭化系统,包括依次相连的进料仓、炉体、粉尘分离器、净化沉降装置、冷凝塔、热解气回收利用装置和热解液收集装置,进料仓设置进料口,进料仓与炉体的入口相连通,炉体具有加热元件,加热元件能够对炉体内的物料进行加热,炉体的出口与粉尘分离器的入口相连通,炉体可转动地与粉尘分离器相连,粉尘分离器的出口与净化沉降装置的入口相连通,净化沉降装置的气体出口与冷凝塔的入口相连通,冷凝塔的气体出口与热解气回收利用装置的入口相连通,净化沉降装置的液体出口、冷凝塔的液体出口、热解气回收利用装置的液体出口均与热解液收集装置相连通;炉体还连接有电控单元,电控单元能够控制炉体的转速并监测炉体内的温度。本发明的生物质热解炭化系统,物料由进料仓加入,继而进入炉体中,炉体旋转并加热物料,物料热解,粉尘分离器能够分离热解过程中的产物和原料粉尘,热解产生的蒸汽进入净化沉降装置中,净化沉降装置能够对热解蒸汽进行净化与沉降,净化后的热解蒸汽进入冷凝塔中,冷凝塔冷却热解蒸汽,分离热解气和热解液,热解气回收利用装置能够收集分离出的热解气,热解液进入热解液收集装置,电控单元能够控制炉体的转速并监测炉体内热解温度。利用本发明的生物质热解炭化系统,能够准确测定和控制热解不同阶段的温度,并将热解产物回收,实现生物质炭化过程零排放、零污染,本发明的系统结构紧凑、操作方便,降低了操作人员劳动负担。Compared with the prior art, the present invention achieves the following technical effects: the biomass pyrolysis carbonization system of the present invention includes a feed bin, a furnace body, a dust separator, a purification settling device, a condensation tower, and a pyrolysis gas recycling and utilization that are connected in sequence. The device and the pyrolysis liquid collection device, the feeding bin is provided with a feeding port, and the feeding bin is connected with the inlet of the furnace body. The furnace body has a heating element, which can heat the materials in the furnace body. The inlet of the separator is connected, the furnace body is rotatably connected with the dust separator, the outlet of the dust separator is connected with the inlet of the purification settling device, the gas outlet of the purification settling device is connected with the inlet of the condensing tower, and the gas of the condensing tower is connected. The outlet is communicated with the inlet of the pyrolysis gas recovery and utilization device, and the liquid outlet of the purification settling device, the liquid outlet of the condensation tower, and the liquid outlet of the pyrolysis gas recovery and utilization device are all communicated with the pyrolysis liquid collection device; the furnace body is also connected with a Electronic control unit, the electronic control unit can control the speed of the furnace body and monitor the temperature in the furnace body. In the biomass pyrolysis carbonization system of the present invention, the material is fed from the feed bin and then enters the furnace body, the furnace body rotates and heats the material, the material is pyrolyzed, and the dust separator can separate the product and the raw material dust in the pyrolysis process. The steam generated by the pyrolysis enters the purification settling device, which can purify and settle the pyrolysis steam. The purified pyrolysis steam enters the condensation tower, which cools the pyrolysis steam and separates the pyrolysis gas and the pyrolysis liquid. The pyrolysis gas recovery and utilization device can collect the separated pyrolysis gas, the pyrolysis liquid enters the pyrolysis liquid collection device, and the electric control unit can control the speed of the furnace body and monitor the pyrolysis temperature in the furnace body. By using the biomass pyrolysis carbonization system of the present invention, the temperature of different stages of pyrolysis can be accurately measured and controlled, and the pyrolysis products can be recovered to realize zero emission and zero pollution in the biomass carbonization process. The system of the present invention has a compact structure and is easy to operate. , reducing the operator's labor burden.

附图说明Description of drawings

为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例中所需要使用的附图作简单地介绍,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性的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the accompanying drawings required in the embodiments will be briefly introduced below. Obviously, the drawings in the following description are only some of the present invention. In the embodiments, for those of ordinary skill in the art, other drawings can also be obtained according to these drawings without creative labor.

图1为本发明的生物质热解炭化系统的结构示意图;Fig. 1 is the structural representation of the biomass pyrolysis carbonization system of the present invention;

图2为本发明的生物质热解炭化系统的俯视图;Fig. 2 is the top view of the biomass pyrolysis carbonization system of the present invention;

其中,1为进料仓,2为炉体,3为粉尘分离器,4为净化沉降装置,5为冷凝塔,6为热解液收集装置,7为热解气回收利用装置,8为加热元件,9为温度传感器,10为电控单元。Among them, 1 is the feed bin, 2 is the furnace body, 3 is the dust separator, 4 is the purification settling device, 5 is the condensation tower, 6 is the pyrolysis liquid collection device, 7 is the pyrolysis gas recycling device, and 8 is the heating Components, 9 is a temperature sensor, 10 is an electronic control unit.

具体实施方式Detailed ways

下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, but not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.

本发明的目的是提供一种生物质热解炭化系统,以解决上述现有技术存在的问题,提高生物质热解炭化工作效率,降低操作人员劳动强度。The purpose of the present invention is to provide a biomass pyrolysis carbonization system, so as to solve the above problems existing in the prior art, improve the biomass pyrolysis carbonization work efficiency, and reduce the labor intensity of operators.

为使本发明的上述目的、特征和优点能够更加明显易懂,下面结合附图和具体实施方式对本发明作进一步详细的说明。In order to make the above objects, features and advantages of the present invention more clearly understood, the present invention will be described in further detail below with reference to the accompanying drawings and specific embodiments.

请参考图1-2,其中,图1为本发明的生物质热解炭化系统的结构示意图,图2为本发明的生物质热解炭化系统的俯视图。Please refer to FIGS. 1-2, wherein, FIG. 1 is a schematic structural diagram of the biomass pyrolysis carbonization system of the present invention, and FIG. 2 is a top view of the biomass pyrolysis carbonization system of the present invention.

本发明提供一种生物质热解炭化系统,包括依次相连的进料仓1、炉体2、粉尘分离器3、净化沉降装置4、冷凝塔5、热解气回收利用装置7和热解液收集装置6,进料仓1设置进料口,进料仓1与炉体2的入口相连通,炉体2具有加热元件8,加热元件8能够对炉体2内的物料进行加热,炉体2的出口与粉尘分离器3的入口相连通,炉体2可转动地与粉尘分离器3相连,粉尘分离器3的出口与净化沉降装置4的入口相连通,净化沉降装置4的气体出口与冷凝塔5的入口相连通,冷凝塔5的气体出口与热解气回收利用装置7的入口相连通,净化沉降装置4的液体出口、冷凝塔5的液体出口、热解气回收利用装置7的液体出口均与热解液收集装置6相连通;炉体2还连接有电控单元10,电控单元10能够控制炉体2的转速并监测炉体2内的温度。The present invention provides a biomass pyrolysis carbonization system, which includes a feed bin 1, a furnace body 2, a dust separator 3, a purification settling device 4, a condensation tower 5, a pyrolysis gas recovery and utilization device 7 and a pyrolysis liquid, which are connected in sequence. The collection device 6, the feeding bin 1 is provided with a feeding port, and the feeding bin 1 is communicated with the inlet of the furnace body 2. The furnace body 2 has a heating element 8, and the heating element 8 can heat the materials in the furnace body 2. The furnace body The outlet of 2 is communicated with the inlet of the dust separator 3, the furnace body 2 is rotatably connected with the dust separator 3, the outlet of the dust separator 3 is communicated with the inlet of the purification settling device 4, and the gas outlet of the purification settling device 4 is connected with the dust separator 3. The inlet of the condensation tower 5 is communicated, the gas outlet of the condensation tower 5 is communicated with the inlet of the pyrolysis gas recovery and utilization device 7, the liquid outlet of the purification settling device 4, the liquid outlet of the condensation tower 5, the pyrolysis gas recovery and utilization device 7 are communicated. The liquid outlets are all communicated with the pyrolysis liquid collecting device 6 ; the furnace body 2 is also connected with an electronic control unit 10 , which can control the rotational speed of the furnace body 2 and monitor the temperature in the furnace body 2 .

本发明的生物质热解炭化系统,物料由进料仓1加入,继而进入炉体2中,炉体2旋转并加热物料,物料热解,粉尘分离器3能够分离热解过程中的产物和原料粉尘,热解产生的蒸汽进入净化沉降装置4中,净化沉降装置4能够对热解蒸汽进行净化与沉降,净化后的热解蒸汽进入冷凝塔5中,冷凝塔5冷却热解蒸汽,分离热解气和热解液,热解气回收利用装置7能够收集分离出的热解气,热解液进入热解液收集装置6,电控单元10能够控制炉体2的转速并监测炉体2内热解温度,利用本发明的生物质热解炭化系统,能够准确测定和控制热解不同阶段的温度,并将热解产物回收,实现生物质炭化过程零排放、零污染,本发明的系统结构紧凑、操作方便,降低了操作人员劳动负担。In the biomass pyrolysis carbonization system of the present invention, the material is fed from the feed bin 1, and then enters the furnace body 2, the furnace body 2 rotates and heats the material, the material is pyrolyzed, and the dust separator 3 can separate the products in the pyrolysis process and The raw material dust and the steam generated by pyrolysis enter the purification and sedimentation device 4. The purification and sedimentation device 4 can purify and settle the pyrolysis steam. The purified pyrolysis steam enters the condensation tower 5, and the condensation tower 5 cools the pyrolysis steam and separates it. Pyrolysis gas and pyrolysis liquid, the pyrolysis gas recovery and utilization device 7 can collect the separated pyrolysis gas, the pyrolysis liquid enters the pyrolysis liquid collection device 6, and the electronic control unit 10 can control the speed of the furnace body 2 and monitor the furnace body. 2. Internal pyrolysis temperature, the biomass pyrolysis carbonization system of the present invention can accurately measure and control the temperature of different stages of pyrolysis, and the pyrolysis products can be recovered to achieve zero emission and zero pollution in the biomass carbonization process. The system has compact structure and convenient operation, which reduces the labor burden of operators.

具体地,炉体2包括外壳和内胆,炉体2为分体式结构,能够减少热解过程中的温度损失,外壳和内胆采用耐高温合金材料职称,不易变形,内胆可转动地设置于外壳内,加热元件8能够加热内胆内的物料,内胆内设置温度传感器9,温度传感器9与电控单元10信号相连,温度传感器9能够计量热解温度,温度传感器9能够监测炉体2轴线处温度,更加真实有效地反映热解温度。Specifically, the furnace body 2 includes an outer shell and an inner liner. The furnace body 2 is a split structure, which can reduce the temperature loss during the pyrolysis process. The outer shell and the inner liner are made of high-temperature resistant alloy materials, which are not easily deformed. In the outer shell, the heating element 8 can heat the material in the inner tank, and a temperature sensor 9 is arranged in the inner tank. The temperature sensor 9 is connected with the signal of the electronic control unit 10, the temperature sensor 9 can measure the pyrolysis temperature, and the temperature sensor 9 can monitor the furnace body. The temperature at the 2 axis reflects the pyrolysis temperature more realistically and effectively.

为了使炉体2内的物料能够充分旋转受热,内胆的内壁上设置旋转片,旋转片倾斜设置,旋转片能够使物料充分旋转受热,并避免物料相互粘连而导致热解不充分,除此之外,在生物炭回收阶段可通过内胆带动旋转片旋转自动分离热解炭。In order to make the materials in the furnace body 2 fully rotate and heat, a rotating plate is arranged on the inner wall of the inner tank, and the rotating plate is inclined. In addition, in the biochar recovery stage, the inner tank can drive the rotary plate to rotate and automatically separate the pyrolysis carbon.

在本具体实施方式中,旋转片为四边形板状结构,旋转片与内胆焊接相连。In this specific embodiment, the rotating piece is a quadrilateral plate-like structure, and the rotating piece is connected to the inner pot by welding.

为了进一步提高物料旋转受热均匀性,旋转片的数量为若干组,每组旋转片的数量为多片,多片旋转片绕内胆的轴线周状均布,若干组旋转片沿内胆的轴线等间距均布,相邻组的旋转片交错设置,提高物料旋转受热的均匀性。In order to further improve the uniformity of the rotation and heating of the material, the number of rotating pieces is several groups, and the number of each group of rotating pieces is multiple pieces. The multiple pieces of rotating pieces are evenly distributed around the axis of the inner tank, and several groups of rotating pieces are along the axis of the inner tank. Equally spaced and evenly distributed, the rotating plates of adjacent groups are staggered to improve the uniformity of material rotation and heating.

在本发明的其他实施方式中,旋转片的数量为三组,每组旋转片的数量为四片,旋转片的总数量为十二片。In other embodiments of the present invention, the number of rotating plates is three groups, the number of rotating plates in each group is four, and the total number of rotating plates is twelve.

更具体地,净化沉降装置4的数量、冷凝塔5的数量均为两组,两组净化沉降装置4串联设置,两组冷凝塔5串联设置,净化沉降装置4和冷凝塔5的数量均为两组串联设置,提高热解蒸汽的净化沉降以及冷凝效率,在本具体实施方式中,冷凝塔5采用水冷方式冷却热解蒸汽。另外,在净化沉降装置4和冷凝塔5的底部均设置可控开关,不仅可随时观测产物状态,对事故快速检修也提供了一定帮助。More specifically, the number of purification settling devices 4 and the number of condensation towers 5 are two groups, two groups of purification settling devices 4 are arranged in series, and two groups of condensing towers 5 are arranged in series, and the number of purification settling devices 4 and condensation towers 5 are both. The two groups are arranged in series to improve the purification, sedimentation and condensation efficiency of the pyrolysis steam. In this specific embodiment, the condensation tower 5 uses a water cooling method to cool the pyrolysis steam. In addition, controllable switches are set at the bottom of the purification settling device 4 and the condensing tower 5, which can not only observe the state of the product at any time, but also provide certain help for the rapid maintenance of accidents.

进一步地,净化沉降装置4的气体出口位于净化沉降装置4的顶部,冷凝塔5的气体出口位于冷凝塔5的顶部,净化沉降装置4的液体出口位于净化沉降装置4的底部,冷凝塔5的液体出口位于冷凝塔5的底部,便于热解蒸汽和热解液顺利输送。Further, the gas outlet of the purification settling device 4 is located at the top of the purification settling device 4, the gas outlet of the condensation tower 5 is located at the top of the condensation tower 5, the liquid outlet of the purification settling device 4 is located at the bottom of the purification settling device 4, and the gas outlet of the condensation tower 5 is located at the bottom of the purification settling device 4. The liquid outlet is located at the bottom of the condensation tower 5, which is convenient for the smooth transportation of pyrolysis steam and pyrolysis liquid.

还需要强调的是,加热元件8采用燃气加热方式,热解气回收利用装置7与加热元件8相连通,物料热解产生的燃气可用于热解加热,减少输入性燃气消耗量,不仅可以使系统达到一个相对平衡又可随时观测热解气燃烧情况进而判断其有效成分,对进行实验时的数据记录有很大帮助。It should also be emphasized that the heating element 8 is heated by gas, and the pyrolysis gas recovery and utilization device 7 is connected to the heating element 8. The gas generated by the pyrolysis of materials can be used for pyrolysis heating, reducing the consumption of input gas, not only making The system achieves a relative balance and can observe the combustion of pyrolysis gas at any time to determine its effective components, which is of great help for data recording during experiments.

本发明的生物质热解炭化系统,人工粉碎处理物料后由进料口添加入进料仓1中,继而进入炉体2内,炉体2通过驱动器带动其旋转,驱动器与电控单元10相连,炉体2旋转保证物料热解期间受热均匀,提高热解效率与质量。为保证热解时间内物料充分热解,物料始终位于炉体2内部,热解结束后,通过旋转炉体2加速生物炭散热,冷却至室温后收集防潮袋中。控制炉体2旋转速度可加速生物炭散热,减少热解结束到生物炭收集的等待时间;通过炉体2旋转可驱动热解炭向炉体2出口位置移动,便于生物炭收集。In the biomass pyrolysis carbonization system of the present invention, the materials are manually pulverized and added into the feed bin 1 through the feed port, and then into the furnace body 2. The furnace body 2 is driven to rotate by a driver, and the driver is connected to the electronic control unit 10. , the furnace body 2 rotates to ensure that the material is heated evenly during the pyrolysis period, and the pyrolysis efficiency and quality are improved. In order to ensure that the material is fully pyrolyzed within the pyrolysis time, the material is always located inside the furnace body 2. After the pyrolysis is completed, the biochar is accelerated to dissipate heat by rotating the furnace body 2, and is collected in a moisture-proof bag after cooling to room temperature. Controlling the rotation speed of the furnace body 2 can accelerate the heat dissipation of the biochar and reduce the waiting time from the end of the pyrolysis to the collection of the biochar; the rotation of the furnace body 2 can drive the pyrolysis carbon to move to the outlet of the furnace body 2 to facilitate the collection of the biochar.

热解产生的焦油蒸汽同木醋液蒸汽共同进入净化沉降装置4,此时焦油与部分木醋液冷凝为液体状,其中大部分焦油可通过第一组净化沉降装置4底部的控制开关收集(由于实验热解原料较少,焦油产量低,故采用方形容器收集,大型生产工作中可单独设置焦油收集容器),少部分随木醋液进入液体收集阶段冷却放置后可分离。炉体2的内胆封闭,热解过程中蒸汽状产物受气压影响由炉体2的出口随管道向后续装置移动。The tar vapor that the pyrolysis produces enters the purification settling device 4 together with the wood vinegar vapor, and the tar and part of the wood vinegar are condensed into a liquid state at this time, and most of the tars can be collected by the control switch at the bottom of the first group purification settling device 4 ( Due to less raw materials and low tar yield in the experiment, a square container is used for collection, and a tar collection container can be set up separately in large-scale production work. The inner liner of the furnace body 2 is closed, and during the pyrolysis process, the steam-like product is affected by the air pressure and moves from the outlet of the furnace body 2 to the subsequent device along with the pipeline.

通过冷凝塔5对木醋液进行冷却,大部分焦油已通过第一组冷凝塔5收集,此时冷凝塔5冷凝所得到的木醋液浓度较高,纯度较好。冷凝塔5连接有动力水泵和水冷管道,采用冷却水循环的方式对热解产物进行冷却。The wood vinegar liquid is cooled by the condensation tower 5, most of the tar has been collected by the first group of condensation towers 5, and the wood vinegar liquid concentration obtained by the condensation tower 5 condensation is higher now, and the purity is better. The condensing tower 5 is connected with a power water pump and a water cooling pipeline, and the pyrolysis product is cooled by means of cooling water circulation.

热解产生的热解气体通过冷却、淋溶后进入气体回收利用装置,同时为热解提供能量。热解气作为辅助燃料提供热解能量,既可减少外源燃料输入,同时可观测热解气燃烧火焰性状,为实验提供参考数据。The pyrolysis gas generated by pyrolysis enters the gas recovery and utilization device after cooling and leaching, and provides energy for pyrolysis at the same time. The pyrolysis gas is used as an auxiliary fuel to provide pyrolysis energy, which can not only reduce the input of external fuel, but also observe the combustion flame properties of the pyrolysis gas, providing reference data for the experiment.

本发明中应用了具体个例对本发明的原理及实施方式进行了阐述,以上实施例的说明只是用于帮助理解本发明的方法及其核心思想;同时,对于本领域的一般技术人员,依据本发明的思想,在具体实施方式及应用范围上均会有改变之处。综上所述,本说明书内容不应理解为对本发明的限制。In the present invention, specific examples are used to illustrate the principles and implementations of the present invention, and the descriptions of the above embodiments are only used to help understand the method and the core idea of the present invention; There will be changes in the specific implementation manner and application scope of the idea of the invention. In conclusion, the contents of this specification should not be construed as limiting the present invention.

Claims (9)

1.一种生物质热解炭化系统,其特征在于:包括依次相连的进料仓、炉体、粉尘分离器、净化沉降装置、冷凝塔、热解气回收利用装置和热解液收集装置,所述进料仓设置进料口,所述进料仓与所述炉体的入口相连通,所述炉体具有加热元件,所述加热元件能够对所述炉体内的物料进行加热,所述炉体的出口与所述粉尘分离器的入口相连通,所述炉体可转动地与所述粉尘分离器相连,所述粉尘分离器的出口与所述净化沉降装置的入口相连通,所述净化沉降装置的气体出口与所述冷凝塔的入口相连通,所述冷凝塔的气体出口与所述热解气回收利用装置的入口相连通,所述净化沉降装置的液体出口、所述冷凝塔的液体出口、所述热解气回收利用装置的液体出口均与所述热解液收集装置相连通;所述炉体还连接有电控单元,所述电控单元能够控制所述炉体的转速并监测所述炉体内的温度。1. a biomass pyrolysis carbonization system, it is characterized in that: comprise successively connected feed bins, furnace bodies, dust separators, purification settling devices, condensation towers, pyrolysis gas recycling devices and pyrolysis liquid collection devices, The feeding bin is provided with a feeding port, and the feeding bin is communicated with the inlet of the furnace body. The furnace body has a heating element, and the heating element can heat the materials in the furnace body. The outlet of the furnace body is communicated with the inlet of the dust separator, the furnace body is rotatably connected to the dust separator, the outlet of the dust separator is communicated with the inlet of the purification sedimentation device, the The gas outlet of the purification sedimentation device is communicated with the inlet of the condensation tower, the gas outlet of the condensation tower is communicated with the inlet of the pyrolysis gas recycling device, the liquid outlet of the purification sedimentation device, the condensation tower The liquid outlet of the furnace and the liquid outlet of the pyrolysis gas recovery and utilization device are all communicated with the pyrolysis liquid collection device; the furnace body is also connected with an electric control unit, which can control the operation of the furnace body. speed and monitor the temperature inside the furnace. 2.根据权利要求1所述的生物质热解炭化系统,其特征在于:所述炉体包括外壳和内胆,所述内胆可转动地设置于所述外壳内,所述加热元件能够加热所述内胆内的物料,所述内胆内设置温度传感器,所述温度传感器与所述电控单元信号相连。2 . The biomass pyrolysis carbonization system according to claim 1 , wherein the furnace body comprises an outer shell and an inner liner, the inner liner is rotatably arranged in the outer shell, and the heating element is capable of heating For the material in the inner tank, a temperature sensor is arranged in the inner tank, and the temperature sensor is signally connected to the electronic control unit. 3.根据权利要求2所述的生物质热解炭化系统,其特征在于:所述内胆的内壁上设置旋转片,所述旋转片倾斜设置。3 . The biomass pyrolysis carbonization system according to claim 2 , wherein a rotating plate is arranged on the inner wall of the inner tank, and the rotating plate is inclined. 4 . 4.根据权利要求3所述的生物质热解炭化系统,其特征在于:所述旋转片为四边形板状结构。4 . The biomass pyrolysis carbonization system according to claim 3 , wherein the rotating plate has a quadrangular plate-like structure. 5 . 5.根据权利要求3所述的生物质热解炭化系统,其特征在于:所述旋转片的数量为若干组,每组所述旋转片的数量为多片,多片所述旋转片绕所述内胆的轴线周状均布,若干组所述旋转片沿所述内胆的轴线等间距均布。5 . The biomass pyrolysis carbonization system according to claim 3 , wherein the number of the rotating blades is several groups, the number of the rotating blades in each group is multiple, and the rotating blades are wound around the The axis of the inner pot is evenly distributed around the circumference, and several groups of the rotating sheets are evenly distributed along the axis of the inner pot at equal intervals. 6.根据权利要求5所述的生物质热解炭化系统,其特征在于:所述旋转片的数量为三组,每组所述旋转片的数量为四片。6 . The biomass pyrolysis carbonization system according to claim 5 , wherein the number of the rotating blades is three groups, and the number of the rotating blades in each group is four. 7 . 7.根据权利要求1所述的生物质热解炭化系统,其特征在于:所述净化沉降装置的数量、所述冷凝塔的数量均为两组,两组所述净化沉降装置串联设置,两组所述冷凝塔串联设置。7 . The biomass pyrolysis carbonization system according to claim 1 , wherein the number of the purification settling devices and the number of the condensation towers are two groups, and the two groups of the purification settling devices are arranged in series, and the two groups are arranged in series. 8 . The condensing towers are arranged in series. 8.根据权利要求7所述的生物质热解炭化系统,其特征在于:所述净化沉降装置的气体出口位于净化沉降装置的顶部,所述冷凝塔的气体出口位于所述冷凝塔的顶部,所述净化沉降装置的液体出口位于所述净化沉降装置的底部,所述冷凝塔的液体出口位于所述冷凝塔的底部。8. The biomass pyrolysis carbonization system according to claim 7, characterized in that: the gas outlet of the purification sedimentation device is located at the top of the purification sedimentation device, and the gas outlet of the condensation tower is located at the top of the condensation tower, The liquid outlet of the purification sedimentation device is located at the bottom of the purification sedimentation device, and the liquid outlet of the condensation tower is located at the bottom of the condensation tower. 9.根据权利要求1-8任一项所述的生物质热解炭化系统,其特征在于:所述加热元件采用燃气加热方式,所述热解气回收利用装置与所述加热元件相连通。9 . The biomass pyrolysis carbonization system according to claim 1 , wherein the heating element adopts a gas heating method, and the pyrolysis gas recovery and utilization device is communicated with the heating element. 10 .
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103980921A (en) * 2014-05-29 2014-08-13 曹文祥 Process for producing fuel oil by thermal cracking of biomass
CN204079889U (en) * 2014-08-19 2015-01-07 广东天源环境科技有限公司 A kind of pyrolysis plant of organic solid waste process
KR101902234B1 (en) * 2018-07-05 2018-09-28 (주)오엔앰 코리아 Screw-type Reactor for Biomass Torrefaction
CN208748006U (en) * 2018-07-11 2019-04-16 北京三聚绿能科技有限公司 A kind of biomass pyrolytic charing furnace
CN109762578A (en) * 2019-03-21 2019-05-17 深圳市中粤华远科技有限公司 Continuous solid waste material microwave carbonizing plant and its working method

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103980921A (en) * 2014-05-29 2014-08-13 曹文祥 Process for producing fuel oil by thermal cracking of biomass
CN204079889U (en) * 2014-08-19 2015-01-07 广东天源环境科技有限公司 A kind of pyrolysis plant of organic solid waste process
KR101902234B1 (en) * 2018-07-05 2018-09-28 (주)오엔앰 코리아 Screw-type Reactor for Biomass Torrefaction
CN208748006U (en) * 2018-07-11 2019-04-16 北京三聚绿能科技有限公司 A kind of biomass pyrolytic charing furnace
CN109762578A (en) * 2019-03-21 2019-05-17 深圳市中粤华远科技有限公司 Continuous solid waste material microwave carbonizing plant and its working method

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
B.A.马泽里: "《轻金属冶炼 第一册(氧化铝)》", 30 July 1961, 中国工业出版社 *
吴启成: "《油页岩干馏技术》", 31 March 2012, 辽宁科学技术出版社 *
黄振兴: "《活性炭技术基础》", 30 June 2006, 兵器工业出版社 *

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Application publication date: 20200918