WO2022152311A1

WO2022152311A1 - Waste gas/waste liquid/solid waste combustion treatment device and use method therefor

Info

Publication number: WO2022152311A1
Application number: PCT/CN2022/072508
Authority: WO
Inventors: 牛芳; 王翰锋; 王鹏涛; 张红顺; 刘鹏中; 石亮; 龚艳艳; 裘星; 纪任山; 罗伟; 梁兴; 刘刚; 魏琰荣; 贾楠; 王志星; 郑祥玉; 闫黎黎; 刘振宇; 苗鹏; 颜淑娟
Original assignee: 煤科院节能技术有限公司
Priority date: 2021-01-18
Filing date: 2022-01-18
Publication date: 2022-07-21

Abstract

A waste gas/waste liquid/solid waste combustion treatment device (100), comprising a housing (101), a feeding assembly (5), and air guide cylinders. The housing (101) is provided with a first cavity (102) and a circumferential wall (103) surrounding the first cavity (102); the first cavity (102) comprises an air guide cavity, a combustion stabilization cavity (1021), and a rectification cavity (1022) that are sequentially communicated; the feeding assembly (5) is provided in the first cavity (102); there are multiple air guide cylinders that are all provided in the first cavity (102); channels are formed between the housing (101) and the air guide cylinder adjacent thereto, between the feeding assembly (5) and the air guide cylinder adjacent thereto, and between two adjacent air guide cylinders. The combustion treatment device (100) can perform effective and full combustion treatment on waste gas, waste liquid, and solid waste. Also disclosed is a use method for the combustion treatment device (100).

Description

废气/废液/固废燃烧处理器及其使用方法Exhaust gas/waste liquid/solid waste combustion processor and method of use

相关申请的交叉引用CROSS-REFERENCE TO RELATED APPLICATIONS

本申请要求申请号为202120131552.1，202110064059.7，202120131544.7，202120131542.8，202110062299.3，202120131555.5，202110062281.3，202110064060.X、申请日为2021年1月18日的中国专利申请的优先权和权益，上述中国专利申请的全部内容在此通过引用并入本申请。本申请要求申请号为202120131552.1，202110064059.7，202120131544.7，202120131542.8，202110062299.3，202120131555.5，202110062281.3，202110064060.X、申请日为2021年1月18日的中国专利申请的优先权和权益，上述中国专利申请的全部内容This application is hereby incorporated by reference.

技术领域technical field

本申请涉及废物处理技术领域，尤其涉及一种废气/废液/固废燃烧处理器及其使用方法。The present application relates to the technical field of waste treatment, and in particular, to a waste gas/waste liquid/solid waste combustion processor and a method of using the same.

背景技术Background technique

有机废液、工业废气和固废的处理是生产生活中需要解决的重要问题，其中,有机废液广泛存在于基础化学原料制造、煤化工、石油化工等行业，为高浓度含盐污染性废液，产生量巨大，组分复杂且物化特性特殊，比如热值低、灰熔点低、腐蚀性物质含量高等，对化工有机废液处理目前基本使用有化学反应法、物理分离法、填埋法和燃烧处理，其中燃烧处理是一种较为通用的低成本、低污染方式，但处理过程中仍存在难燃、处理效率低、设备寿命短等问题。The treatment of organic waste liquid, industrial waste gas and solid waste is an important problem that needs to be solved in production and life. Among them, organic waste liquid widely exists in basic chemical raw material manufacturing, coal chemical industry, petrochemical industry and other industries, and is a high-concentration salt-containing pollution waste. The production volume is huge, the components are complex and the physicochemical properties are special, such as low calorific value, low ash melting point, high content of corrosive substances, chemical reaction method, physical separation method, landfill method are basically used for the treatment of chemical organic waste liquid. And combustion treatment, in which combustion treatment is a relatively common low-cost and low-pollution method, but there are still problems such as flame retardancy, low treatment efficiency, and short equipment life in the treatment process.

含氟化物的废气对大气环境和人体的危害性较严重，针对含氟化物的废气的处理方法主要采用燃烧处理，含氟化物的废气在燃烧后可分解为可直接回收处理的气体或可直接排放的气体。但现有的工业废气燃烧处理设备存在着体积庞大、处理力度小、反应不完全等问题。The waste gas containing fluoride is more harmful to the atmospheric environment and human body. The treatment method for waste gas containing fluoride mainly adopts combustion treatment. After combustion, the waste gas containing fluoride can be decomposed into gas that can be directly recycled or processed directly. emitted gas. However, the existing industrial waste gas combustion and treatment equipment has problems such as bulky volume, small processing power, and incomplete reaction.

垃圾焚烧飞灰的处理方式主要包括固化稳定处理技术、化学处理与热处理技术。但固化稳定处理技术和化学处理技术具有处理成本较高、操作复杂、稳定作用小及有害物质易浸出等问题。而热处理技术也存在垃圾焚烧燃烧不充分，热处理设备内壁积灰结焦和腐蚀等问题。The treatment methods of waste incineration fly ash mainly include solidification and stabilization treatment technology, chemical treatment and heat treatment technology. However, the curing and stabilization treatment technology and chemical treatment technology have problems such as high treatment cost, complicated operation, small stabilization effect, and easy leaching of harmful substances. The heat treatment technology also has problems such as insufficient waste incineration and combustion, ash deposition, coking and corrosion on the inner wall of the heat treatment equipment.

发明内容SUMMARY OF THE INVENTION

本申请旨在至少在一定程度上解决相关技术中的技术问题之一。The present application aims to solve one of the technical problems in the related art at least to a certain extent.

为此，本申请的实施例提出一种废气/废液/固废燃烧处理器，所述燃烧处理器可对废气、废液和固废进行有效的燃烧处理。To this end, the embodiments of the present application propose an exhaust gas/waste liquid/solid waste combustion processor, which can perform efficient combustion treatment on exhaust gas, waste liquid and solid waste.

本申请实施例的废气/废液/固废燃烧处理器包括：The exhaust gas/waste liquid/solid waste combustion processor of the embodiment of the present application includes:

壳体，所述壳体具有第一腔和围成所述第一腔的周壁，所述第一腔包括依次连通的导风腔、稳燃腔和整流腔；a casing, the casing has a first cavity and a peripheral wall surrounding the first cavity, and the first cavity includes an air guide cavity, a combustion stabilization cavity and a rectification cavity that are communicated in sequence;

供料组件，所述供料组件设在所述第一腔内；a feeding assembly, the feeding assembly is arranged in the first cavity;

导风筒，所述导风筒为多个，多个所述导风筒均设在所述所述第一腔内；an air guide tube, there are multiple air guide tubes, and the multiple air guide tubes are all arranged in the first cavity;

所述壳体和与之相邻的所述导风筒之间、所述供料组件和与之相邻的所述导风筒之间、相邻的两个所述导风筒之间形成通道。Formed between the casing and the adjacent air guide tubes, between the feeding assembly and the adjacent air guide tubes, and between the two adjacent air guide tubes aisle.

在一些实施例中，所述导风筒包括：In some embodiments, the air guide includes:

调温导风筒，套设在所述供料组件的进液端，靠近所述供料组件进液端一端敞开，远离所述供料组件进液端一端封闭，所述调温导风筒的内周面与所述供料组件的外周面之间形成过渡通道；A temperature-adjusting air guide tube is sleeved on the liquid inlet end of the feeding assembly, one end close to the liquid inlet end of the feeding assembly is open, and one end away from the liquid inlet end of the feeding assembly is closed. A transition channel is formed between the inner peripheral surface of the feed assembly and the outer peripheral surface of the feeding assembly;

贴壁导风筒，设在所述第一腔内，所述贴壁导风筒的外周面和所述周壁的内周面之间形成贴壁风通道；The wall-adhering air guide tube is arranged in the first cavity, and a wall-adhering air channel is formed between the outer peripheral surface of the wall-adhering air guide tube and the inner peripheral surface of the peripheral wall;

助燃导风筒，设在所述第一腔内，所述助燃导风筒的外周面与所述贴壁导风筒的内周面之间形成助燃风通道；The combustion-supporting air guide is arranged in the first cavity, and a combustion-supporting air channel is formed between the outer peripheral surface of the combustion-supporting air guide and the inner peripheral surface of the wall-mounted air guide;

煤粉输送导风筒，所述煤粉输送导风筒的外周面与所述助燃导风筒的内周面之间、所述煤粉输送导风筒的内周面与所述调温导风筒的外周面之间，两者其中之一为煤粉输送通道，另一为调温通道。The pulverized coal conveying air duct, between the outer peripheral surface of the pulverized coal conveying air duct and the inner peripheral surface of the combustion-supporting air duct, the inner peripheral surface of the pulverized coal conveying air duct and the temperature adjustment guide Between the outer peripheral surfaces of the air duct, one of the two is a coal powder conveying channel, and the other is a temperature adjusting channel.

在一些实施例中，所述供料组件包括有机废液输送管、回流帽和雾化喷嘴组件，所述有机废液输送管与所述第一腔同轴设置，所述回流帽设在所述有机废液输送管的出液端，所述回流帽为筒形，所述回流帽的出口朝向所述有机废液输送管的进液端，所述雾化喷嘴组件设置在所述回流帽的出口处。In some embodiments, the feeding assembly includes an organic waste liquid delivery pipe, a return cap and an atomizing nozzle assembly, the organic waste liquid delivery pipe is coaxial with the first cavity, and the return cap is provided at the The liquid outlet end of the organic waste liquid conveying pipe, the return cap is cylindrical, the outlet of the return cap faces the liquid inlet end of the organic waste liquid conveying pipe, and the atomizing nozzle assembly is arranged on the return cap the exit.

在一些实施例中，所述雾化喷嘴组件包括固定盘，所述固定盘套设在所述有机废液输送管的出液端外侧，所述固定盘的外周面与所述回流帽的出口端内边缘连接，所述固定盘上设置有多个贯穿所述固定盘的喷射孔。In some embodiments, the atomizing nozzle assembly includes a fixed disk, the fixed disk is sleeved on the outside of the liquid outlet end of the organic waste liquid conveying pipe, and the outer peripheral surface of the fixed disk is connected to the outlet of the return cap. The inner edges of the ends are connected, and the fixed plate is provided with a plurality of spray holes penetrating the fixed plate.

在一些实施例中，所述助燃风通道和所述调温通道内均设有轴向叶轮组件。In some embodiments, axial impeller assemblies are provided in both the combustion air passage and the temperature adjustment passage.

在一些实施例中，所述贴壁导风筒包括筒体、套设在所述筒体的外周面上的柔性部和调节组件，所述调节组件包括调节件和密封垫圈，所述筒体上沿所述筒体的周向间隔设置有多个安装孔，每个所述安装孔对应设置一个所述调节件，所述调节组件的第一部分穿过所述柔性部且设在所述安装孔内，所述调节件的第二部分压制在所述柔性部的外周面上，所述密封垫圈设在所述调节件的所述第二部分和所述柔性部的外周面之间。In some embodiments, the wall-adhering air guide tube includes a cylindrical body, a flexible portion sleeved on the outer peripheral surface of the cylindrical body, and an adjustment assembly, the adjustment assembly includes an adjustment member and a sealing gasket, and the cylindrical body A plurality of installation holes are arranged at intervals along the circumference of the cylinder body, and each of the installation holes is correspondingly provided with one of the adjustment pieces, and the first part of the adjustment assembly passes through the flexible part and is arranged in the installation hole. In the hole, the second part of the adjusting member is pressed on the outer peripheral surface of the flexible part, and the sealing gasket is provided between the second part of the adjusting member and the outer peripheral surface of the flexible part.

在一些实施例中，所述调温通道内部设置有点火器和火焰检测器。In some embodiments, an igniter and a flame detector are arranged inside the temperature regulation channel.

在一些实施例中，所述煤粉输送通道内侧沿其周向设置有多个浓淡分离结构件。In some embodiments, the inner side of the pulverized coal conveying channel is provided with a plurality of concentration separation structures along the circumference thereof.

本申请第二方面实施例的燃烧处理器的使用方法包括以下步骤：The method for using the combustion processor according to the embodiment of the second aspect of the present application includes the following steps:

S1、根据有机废液的热值及废液量及煤种选择合适直径的所述有机废液输送管、合适雾化特性的所述雾化喷嘴组件及所述浓淡分离组件；S1, according to the calorific value of the organic waste liquid, the amount of waste liquid and the coal type, select the organic waste liquid conveying pipe of suitable diameter, the atomization nozzle assembly with suitable atomization characteristics, and the concentration separation assembly;

S2、分两路通入空气，一路空气经助燃风通道和调温通道进入所述第一腔，另一路经贴壁风通道进入所述第一腔；S2, the air is introduced into two paths, one air enters the first cavity through the combustion-supporting air channel and the temperature adjustment channel, and the other air enters the first cavity through the wall-mounted air channel;

S3、与步骤S2同时进行，煤粉气流点火后经煤粉输送通道进入第一腔；S3, performed simultaneously with step S2, the pulverized coal gas flow enters the first cavity through the pulverized coal conveying channel after ignition;

S4、通入有机废液，有机废液经有机废液输送管进入回流帽，然后经回流帽上的雾化喷嘴组件喷入第一腔。S4. The organic waste liquid is introduced, and the organic waste liquid enters the return cap through the organic waste liquid conveying pipe, and is then sprayed into the first cavity through the atomizing nozzle assembly on the return cap.

在一些实施例中，步骤S2中可同时向调温通道内通入氧化性气体或惰性气体，以维持所述第一腔内的温度在700～1600℃之间。In some embodiments, in step S2, an oxidizing gas or an inert gas may be introduced into the temperature adjustment channel at the same time, so as to maintain the temperature in the first chamber between 700°C and 1600°C.

在一些实施例中，有机废液的入口压力大于所述第一腔内部的压力，控制在0.3～0.5MPa。In some embodiments, the inlet pressure of the organic waste liquid is greater than the pressure inside the first chamber, and is controlled at 0.3-0.5 MPa.

贴壁导风筒，所述贴壁导风筒设在所述第一腔内，所述贴壁导风筒的外周面和所述周壁之间形成贴壁风通道；a wall-adhering air guide tube, the wall-adhering air guide tube is arranged in the first cavity, and a wall-adhering air channel is formed between the outer peripheral surface of the wall-adhering air guide tube and the peripheral wall;

调温导风筒，所述调温导风筒设在所述第一腔内，所述调温导风筒的外周面与所述贴壁导风筒的内周面之间形成调温通道；A temperature-adjusting air duct, the temperature-adjusting air duct is arranged in the first cavity, and a temperature-adjusting channel is formed between the outer peripheral surface of the temperature-adjusting air duct and the inner peripheral surface of the wall-mounted air duct ;

废气输送导风筒，所述废气输送导风筒设在所述第一腔内，所述废气输送导风筒套设在所述供料组件上，所述废气输送导风筒的内周面与所述供料组件的外周面之间形成过渡通道，所述废气输送导风筒的外周面与所述调温导风筒的内周面之间形成废气通道The exhaust gas conveying air guide tube, the exhaust gas conveying air guide tube is arranged in the first cavity, the exhaust gas conveying air guide tube is sleeved on the feeding component, and the inner peripheral surface of the exhaust gas conveying air guide tube is A transition channel is formed between the outer peripheral surface of the feeding assembly, and an exhaust gas channel is formed between the outer peripheral surface of the exhaust gas conveying air guide tube and the inner peripheral surface of the temperature adjustment air guide tube

助燃导风筒，所述助燃导风筒设在所述第一腔内，所述助燃导风筒在内外方向上位于所述贴壁导风筒和所述调温导风筒之间，所述助燃导风筒的外周面和所述贴壁导风筒的内周面之间形成助燃风通道，所述助燃导风筒的内周面和所述调温导风筒的外周面之间形成调温通道。Combustion-supporting air duct, the combustion-supporting air duct is arranged in the first cavity, and the combustion-supporting air duct is located between the wall-mounted air duct and the temperature-adjusting air duct in the inner and outer directions, so A combustion-supporting air channel is formed between the outer peripheral surface of the combustion-supporting air guide tube and the inner peripheral surface of the wall-mounted air guide tube, and a combustion-supporting air channel is formed between the inner peripheral surface of the combustion-supporting air guide tube and the outer peripheral surface of the temperature-adjusting air guide tube. Form a temperature control channel.

在一些实施例中，所述供料组件包括煤粉管和回流帽，所述煤粉管沿所述第一腔的轴线设在所述第一腔内，所述煤粉管具有入口端和出口端，所述废气输送导风筒套设在所述煤粉管的入口端处，所述回流帽设在所述煤粉管的出口端，所述回流帽大体为筒形，所述回流帽的出口朝向所述煤粉管的入口端。In some embodiments, the feed assembly includes a pulverized coal tube and a return cap, the pulverized coal tube disposed within the first cavity along an axis of the first cavity, the pulverized coal tube having an inlet end and a return cap. At the outlet end, the exhaust gas conveying air guide tube is sleeved at the inlet end of the pulverized coal pipe, and the return cap is arranged at the outlet end of the pulverized coal pipe. The outlet of the cap is towards the inlet end of the pulverized coal tube.

在一些实施例中，燃烧处理器进一步包括叶轮组件，所述助燃风通道、所述调温通道和所述废气通道内均设有所述叶轮组件，所述叶轮组件包括彼此相连的叶片和伸缩杆，所述伸缩杆沿所述第一腔的轴向设置。In some embodiments, the combustion processor further includes an impeller assembly, and the impeller assembly is arranged in the combustion air passage, the temperature adjustment passage and the exhaust gas passage, and the impeller assembly includes blades connected to each other and a telescopic and the telescopic rod is arranged along the axial direction of the first cavity.

在一些实施例中，所述贴壁导风筒包括筒体和套设在所述筒体的外周面上的柔性部，所述燃烧处理器进一步包括调节组件，所述调节组件包括调节件和密封垫圈，所述筒体上设有安装孔，所述调节件的第一部分穿过所述柔性部且设在所述安装孔内，所述调节件的第二部分压制在所述柔性部的外周面上，所述密封垫圈设在所述调节件的所述第二部分和所述柔性部的外周面之间。In some embodiments, the wall-adhering air guide tube includes a tube body and a flexible portion sleeved on the outer peripheral surface of the tube body, and the combustion processor further includes an adjustment assembly, and the adjustment assembly includes an adjustment member and A sealing gasket, an installation hole is provided on the cylinder body, a first part of the adjustment piece passes through the flexible part and is arranged in the installation hole, and a second part of the adjustment piece is pressed against the flexible part. On the outer peripheral surface, the sealing gasket is provided between the second portion of the adjusting member and the outer peripheral surface of the flexible portion.

在一些实施例中，燃烧处理器进一步包括煤粉分离器，所述煤粉分离器设在所述煤粉管的入口端，所述煤粉分离器为喉口形分离器、齿轮形分离器或花瓣形分离器。In some embodiments, the combustion processor further comprises a pulverized coal separator, the pulverized coal separator is provided at the inlet end of the pulverized coal pipe, and the pulverized coal separator is a throat-shaped separator, a gear-shaped separator or Petal-shaped separator.

在一些实施例中，所述废气输送导风筒具有沿所述煤粉管的轴向相对设置的第一端和第二端，所述废气输送导风筒的第一端敞开，所述废气输送导风筒的第二端上设有多个通孔，所述燃烧处理器进一步包括火焰检测器和点火器，所述火焰检测器和所述点火器设在所述废气输送导风筒内，所述点火器的火焰穿过所述通孔后射入所述第一腔内。In some embodiments, the exhaust gas conveying air duct has a first end and a second end oppositely disposed along the axial direction of the pulverized coal pipe, the first end of the exhaust gas conveying air duct is open, and the exhaust gas A plurality of through holes are arranged on the second end of the conveying air duct, the combustion processor further includes a flame detector and an igniter, and the flame detector and the igniter are arranged in the exhaust gas conveying air duct , the flame of the igniter is injected into the first cavity after passing through the through hole.

本申请第三方面实施例的燃烧器的使用方法包括以下步骤：The method for using the burner according to the embodiment of the third aspect of the present application includes the following steps:

根据废气的热值、气量和所选用的煤种确定燃烧处理器内的燃烧温度；Determine the combustion temperature in the combustion processor according to the calorific value of the exhaust gas, the gas volume and the selected coal type;

废气通过废气通道进入所述燃烧处理器内；Exhaust gas enters into the combustion processor through the exhaust gas passage;

煤粉经过煤粉供料组件进入所述燃烧处理器内；The pulverized coal enters the combustion processor through the pulverized coal feeding component;

空气分成两路进入所述燃烧处理器内，其中，一路空气通过助燃风通道进入所述燃烧处理器内，另一炉空气通过贴壁风通道进入所述燃烧处理器内并形成贴壁风，贴壁风的至少一部分沿所述燃烧处理器的周壁流动形成冷却层；和The air enters the combustion processor in two ways, wherein one air enters the combustion processor through the combustion-supporting air channel, and the other furnace air enters the combustion processor through the wall-adhering air channel and forms the wall-adhering wind, at least a portion of the wall-to-wall wind flows along the peripheral wall of the combustion processor to form a cooling layer; and

点燃所述燃烧处理器内的煤粉和废气。The pulverized coal and exhaust gases within the combustion processor are ignited.

在一些实施例中，当所述燃烧处理器的所述周壁的温度高于预设温度时，压缩所述贴壁导风筒的所述柔性部以扩大所述贴壁风通道的流通面积，可选地，所述预设温度为40℃。In some embodiments, when the temperature of the peripheral wall of the combustion processor is higher than a preset temperature, the flexible portion of the wall-adhering air guide tube is compressed to expand the flow area of the wall-adhering air channel, Optionally, the preset temperature is 40°C.

在一些实施例中，所述使用方法包括：根据所述煤粉的煤种选用对应的煤粉分离器，所述煤粉分离器为喉口形分离器、齿轮形分离器或花瓣形分离器，可选地，所述废气为含有氟化物的废气。In some embodiments, the using method includes: selecting a corresponding pulverized coal separator according to the coal type of the pulverized coal, and the pulverized coal separator is a throat-shaped separator, a gear-shaped separator or a petal-shaped separator, Optionally, the exhaust gas is an exhaust gas containing fluoride.

助燃导风筒，所述助燃导风筒设在所述第一腔内，所述助燃导风筒的外周面与所述贴壁导风筒的内周面之间形成助燃风通道；a combustion-supporting air guide tube, the combustion-supporting air guide tube is arranged in the first cavity, and a combustion-supporting air channel is formed between the outer peripheral surface of the combustion-supporting air guide tube and the inner peripheral surface of the wall-mounted air guide tube;

调温导风筒，所述调温导风筒设在所述第一腔内，所述调温导风筒套设在所述供料组件上，所述调温导风筒的内周面与所述供料组件的外周面之间形成过渡通道，所述调温导风筒的外周面与所述助燃导风筒的内周面之间形成调温通道。The temperature-adjusting air guide tube is arranged in the first cavity, the temperature-adjusting air guide tube is sleeved on the feeding component, and the inner peripheral surface of the temperature-adjusting air guide tube is A transition channel is formed between it and the outer peripheral surface of the feed assembly, and a temperature regulation channel is formed between the outer peripheral surface of the temperature regulation air guide tube and the inner peripheral surface of the combustion-supporting air guide tube.

在一些实施例中，所述供料组件包括煤粉管和回流帽，所述煤粉管沿所述第一腔的轴线设在所述第一腔内，所述煤粉管具有入口端和出口端，所述调温导风筒套设在所述煤粉管的入口端处，所述回流帽设在所述煤粉管的出口端，所述回流帽大体为筒形，所述回流帽的出口朝向所述煤粉管的入口端。In some embodiments, the feed assembly includes a pulverized coal tube and a return cap, the pulverized coal tube disposed within the first cavity along an axis of the first cavity, the pulverized coal tube having an inlet end and a return cap. At the outlet end, the temperature-adjusting air guide tube is sleeved at the inlet end of the pulverized coal pipe, and the return cap is arranged at the outlet end of the pulverized coal pipe. The outlet of the cap is towards the inlet end of the pulverized coal tube.

在一些实施例中，所述燃烧处理器进一步包括叶轮组件，所述助燃风通道和所述调温通道内均设有所述叶轮组件，所述叶轮组件包括彼此相连的叶片和伸缩杆，所述伸缩杆沿所述第一腔的轴向设置。In some embodiments, the combustion processor further includes an impeller assembly, and the impeller assembly is arranged in the combustion air passage and the temperature adjustment passage, and the impeller assembly includes blades and telescopic rods connected to each other, so The telescopic rod is arranged along the axial direction of the first cavity.

在一些实施例中，所述调温导风筒具有沿所述煤粉管的轴向相对设置的第一端和第二端，所述调温导风筒的第一端敞开，所述调温导风筒的第二端上设有多个通孔，所述燃烧处理器进一步包括火焰检测器和点火器，所述火焰检测器和所述点火器设在所述调温导风筒内，所述点火器的火焰穿过所述通孔后射入所述第一腔内。In some embodiments, the temperature regulation air guide tube has a first end and a second end oppositely disposed along the axial direction of the pulverized coal pipe, the first end of the temperature regulation air guide tube is open, and the temperature regulation air guide tube is open. The second end of the temperature-adjusting air duct is provided with a plurality of through holes, the combustion processor further includes a flame detector and an igniter, and the flame detector and the igniter are arranged in the temperature-adjusting air duct , the flame of the igniter is injected into the first cavity after passing through the through hole.

本申请第四方面实施例的燃烧处理器的使用方法包括以下步骤：The method for using the combustion processor according to the embodiment of the fourth aspect of the present application includes the following steps:

根据垃圾焚灰的成分确定所述燃烧处理器的燃烧温度；Determine the combustion temperature of the combustion processor according to the composition of the waste incineration ash;

所述垃圾焚灰和煤粉通过所述煤粉供料组件进入所述燃烧处理器内；The waste incineration ash and pulverized coal enter into the combustion processor through the pulverized coal feeding component;

点燃所述燃烧处理器内的煤粉和所述垃圾焚灰。The pulverized coal and the refuse incineration ash in the combustion processor are ignited.

在一些实施例中，所述使用方法进一步包括：在使所述垃圾焚灰和所述煤粉进入所述燃烧处理器内之前，将不可燃粉体掺混物、所述煤粉和所述垃圾焚灰混合以便利用所述不可燃粉体掺混物吸附所述垃圾焚灰熔融后的重金属元素，可选地，所述垃圾焚灰的质量占所述垃圾焚灰、所述煤粉与所述不可燃粉体掺混物的总质量的20％-80，所述垃圾焚灰的粒径在50-250微米之间，所述煤粉的粒径在50-250微米之间，所述不可燃粉体掺混物的粒径在50-250微米之间。In some embodiments, the method of using further comprises: mixing a non-combustible powder blend, the pulverized coal, and the The refuse incineration ash is mixed so as to utilize the non-combustible powder admixture to absorb the heavy metal elements after the refuse incineration ash is melted. 20%-80% of the total mass of the non-combustible powder mixture, the particle size of the waste incineration ash is between 50-250 microns, and the particle size of the coal powder is between 50-250 microns, so The particle size of the non-combustible powder blend is between 50-250 microns.

在一些实施例中，所述垃圾焚灰的质量占所述垃圾焚灰与煤粉的总质量的20％-80％。In some embodiments, the mass of the refuse incineration ash accounts for 20%-80% of the total mass of the refuse incineration ash and coal powder.

在一些实施例中，当所述燃烧处理器的周壁的温度高于预设温度时，压缩所述贴壁导风筒的所述柔性部以扩大所述贴壁风通道的流通面积，可选地，所述预设温度为40℃。In some embodiments, when the temperature of the peripheral wall of the combustion processor is higher than a preset temperature, the flexible part of the wall-adhering air guide tube is compressed to expand the flow area of the wall-adhering air channel, optionally Preferably, the preset temperature is 40°C.

在一些实施例中，所述燃烧处理器的燃烧温度在900-1600℃。In some embodiments, the combustion temperature of the combustion processor is 900-1600°C.

贴壁导风筒，设在所述第一腔内，所述贴壁导风筒的外周面和所述周壁之间形成贴壁风通道；The wall-adhering air guide tube is arranged in the first cavity, and a wall-adhering air channel is formed between the outer peripheral surface of the wall-adhering air guide tube and the peripheral wall;

过渡导风筒，设在所述第一腔内，所述过渡导风筒套设在所述供料组件上，所述过渡导风筒的内周面与所述供料组件的外周面之间形成过渡通道，所述过渡导风筒的外周面与所述助燃导风筒的内周面之间形成调温通道。The transition air guide tube is arranged in the first cavity, the transition air guide tube is sleeved on the feed assembly, and the inner peripheral surface of the transition air guide tube and the outer peripheral surface of the feed assembly are connected. A transition channel is formed between, and a temperature adjustment channel is formed between the outer peripheral surface of the transition air guide tube and the inner peripheral surface of the combustion-supporting air guide tube.

在一些实施例中，所述供料组件包括风粉管和回流帽，所述风粉管沿所述第一腔的轴线设在所述第一腔内，所述风粉管具有入口端和出口端，所述过渡导风筒套设在所述风粉管的入口端处，所述回流帽设在所述风粉管的出口端，所述回流帽为筒形，所述回流帽的出口朝向所述风粉管的入口端。In some embodiments, the feed assembly includes an air powder pipe and a return cap, the air powder pipe is disposed in the first cavity along the axis of the first cavity, and the air powder pipe has an inlet end and a return cap. At the outlet end, the transition air guide tube is sleeved at the inlet end of the air-powder pipe, and the return cap is disposed at the outlet end of the air-powder pipe. The outlet is towards the inlet end of the air powder duct.

在一些实施例中，所述助燃风通道和所述调温通道内均设有叶轮组件，所述叶轮组件包括彼此相连的叶片和伸缩杆，所述伸缩杆沿所述第一腔的轴向设置。In some embodiments, both the combustion-supporting air channel and the temperature-adjusting channel are provided with impeller assemblies, and the impeller assemblies include blades and telescopic rods that are connected to each other, and the telescopic rods are along the axial direction of the first cavity. set up.

在一些实施例中，所述过渡导风筒具有沿所述风粉管的轴向相对设置的第一端和第二端，所述过渡导风筒的第一端敞开，所述过渡导风筒的第二端上设有多个通孔，所述燃烧处理器进一步包括点火器，所述点火器设在所述过渡导风筒内，所述点火器的火焰穿过所述通孔后射入所述第一腔内。In some embodiments, the transition air guide tube has a first end and a second end oppositely disposed along the axial direction of the air powder pipe, the first end of the transition air guide tube is open, and the transition air guide tube is open. The second end of the tube is provided with a plurality of through holes, the combustion processor further includes an igniter, the igniter is arranged in the transition air guide tube, and after the flame of the igniter passes through the through holes into the first cavity.

在一些实施例中，所述燃烧处理器进一步包括火焰检测器，所述火焰检测器设在所述过渡导风筒内。In some embodiments, the combustion processor further includes a flame detector disposed within the transition air duct.

本申请第五方面实施例的燃烧器的使用方法包括以下步骤：The method for using the burner according to the embodiment of the fifth aspect of the present application includes the following steps:

S1、将生物质粉和煤粉掺混(掺混比20％～100％)；S1. Blend biomass powder and coal powder (mixing ratio 20% to 100%);

S2、点燃点火器；S2, ignite the igniter;

S3、分两路通入空气，一路经助燃风通道进入稳燃腔，另一路经贴壁风通道进入稳燃腔；S3. Enter the air in two ways, one way enters the stable combustion chamber through the combustion-supporting air channel, and the other enters the stable combustion chamber through the wall-mounted air channel;

S4、将掺混后的生物质粉和煤粉经风粉管和回流帽组成的回流通道吹入稳燃腔内；S4, blowing the mixed biomass powder and coal powder into the stable combustion chamber through the return channel composed of the air powder pipe and the return cap;

S5、通过调温通道向稳燃腔内通入氧化性气体或惰性气体。S5, introducing oxidizing gas or inert gas into the combustion stabilization chamber through the temperature regulation channel.

38、根据权利要求37所述的燃烧处理器的使用方法，其特征在于，所述生物质粉和煤粉的粒径为50～250微米。38. The method for using a combustion processor according to claim 37, wherein the particle size of the biomass powder and coal powder is 50-250 microns.

附图说明Description of drawings

图1是本申请实施例1和实施例2的燃烧处理器的示意图。FIG. 1 is a schematic diagram of the combustion processor of Embodiment 1 and Embodiment 2 of the present application.

图2是本申请实施例2的燃烧处理器的剖视图。FIG. 2 is a cross-sectional view of a combustion processor according to Example 2 of the present application.

图3是本申请实施例的燃烧处理器中叶轮组件6的示意图。FIG. 3 is a schematic diagram of the impeller assembly 6 in the combustion processor according to the embodiment of the present application.

图4是本申请实施例的燃烧处理器中调节组件的示意图。FIG. 4 is a schematic diagram of an adjustment component in a combustion processor according to an embodiment of the present application.

图5是本申请实施例的燃烧处理器中喉口形分离器的示意图。FIG. 5 is a schematic diagram of a throat-shaped separator in a combustion processor according to an embodiment of the present application.

图6是本申请实施例的燃烧处理器中齿轮形分离器的示意图。FIG. 6 is a schematic diagram of a gear-shaped separator in a combustion processor according to an embodiment of the present application.

图7是本申请实施例的燃烧处理器中花瓣形分离器的示意图。FIG. 7 is a schematic diagram of a petal-shaped separator in a combustion processor according to an embodiment of the present application.

图8是本申请的实施例的燃烧处理器的另一个角度的示意图。8 is a schematic diagram of another angle of the combustion processor of an embodiment of the present application.

图9是本申请实施例1的燃烧处理器的剖视图。FIG. 9 is a cross-sectional view of the combustion processor of Example 1 of the present application.

图10是本申请实施例1的燃烧处理器中雾化喷嘴组件示意图图。FIG. 10 is a schematic diagram of an atomizing nozzle assembly in the combustion processor of Example 1 of the present application.

图11是图10中所示的雾化喷嘴组件的剖视图。FIG. 11 is a cross-sectional view of the atomizing nozzle assembly shown in FIG. 10 .

图12是本申请实施例3和实施例4的燃烧处理器的示意图。FIG. 12 is a schematic diagram of the combustion processors of Embodiment 3 and Embodiment 4 of the present application.

图13是本申请实施例3的燃烧处理器的剖视图。FIG. 13 is a cross-sectional view of a combustion processor according to Example 3 of the present application.

图14是本申请实施例4的燃烧处理器的剖视图。FIG. 14 is a cross-sectional view of a combustion processor according to Example 4 of the present application.

附图说明：Description of drawings:

燃烧处理器100，burn processor 100,

壳体101，第一腔102，稳燃腔1021，整流腔1022，周壁103， Shell 101, first cavity 102, combustion stabilization cavity 1021, rectification cavity 1022, peripheral wall 103,

贴壁导风筒1，贴壁风通道11，筒体12，柔性部13，安装孔14，The wall-mounted air guide tube 1, the wall-mounted air channel 11, the cylinder body 12, the flexible part 13, the installation hole 14,

调温导风筒2，调温通道21，Temperature regulation air duct 2, temperature regulation channel 21,

废气输送导风筒3，过渡通道31，废气通道32，The exhaust gas conveying air guide tube 3, the transition channel 31, the exhaust gas channel 32,

助燃导风筒4，助燃风通道41，Combustion-supporting air duct 4, combustion-supporting air channel 41,

供料组件5，煤粉管51，回流帽52，有机废液输送管53，固定盘54，喷射孔541，风粉管55，Feeding assembly 5, pulverized coal pipe 51, return cap 52, organic waste liquid conveying pipe 53, fixed plate 54, injection hole 541, air powder pipe 55,

叶轮组件6，叶片61，伸缩杆62， Impeller assembly 6, blade 61, telescopic rod 62,

调节组件7，调节件71，密封垫圈72，Adjustment assembly 7, adjustment piece 71, sealing washer 72,

煤粉分离器8，喉口形分离器81，齿轮形分离器82，花瓣形分离器83。Pulverized coal separator 8, throat-shaped separator 81, gear-shaped separator 82, and petal-shaped separator 83.

煤粉输送导风筒9，煤粉输送通道91。The pulverized coal conveying air guide tube 9 and the pulverized coal conveying channel 91 .

具体实施方式Detailed ways

下面详细描述本申请的实施例，所述实施例的示例在附图中示出。下面通过参考附图描述的实施例是示例性的，旨在用于解释本申请，而不能理解为对本申请的限制。Embodiments of the present application are described in detail below, examples of which are illustrated in the accompanying drawings. The embodiments described below with reference to the accompanying drawings are exemplary, and are intended to be used to explain the present application, but should not be construed as a limitation to the present application.

本申请实施例的废气/废液/固废燃烧处理器100包括壳体101、供料组件5和导风筒，壳体具有第一腔102和围成第一腔102的周壁103，第一腔102包括依次连通的导风腔、稳燃腔1021和整流腔1022，供料组件5设在第一腔102内，导风筒为多个，多个导风筒均设在第一腔102内，壳体101和与之相邻的导风筒之间、供料组件5和与之相邻的导风筒之间、相邻的两个导风筒之间形成通道。The exhaust gas/waste liquid/solid waste combustion processor 100 in the embodiment of the present application includes a casing 101, a feeding assembly 5 and an air guide tube. The casing has a first cavity 102 and a peripheral wall 103 surrounding the first cavity 102. The cavity 102 includes an air guide cavity, a combustion stabilization cavity 1021 and a rectification cavity 1022 which are connected in sequence. The feeding component 5 is arranged in the first cavity 102, and there are multiple air guide tubes, and the plurality of air guide tubes are all arranged in the first cavity 102. Inside, channels are formed between the housing 101 and the adjacent air guide tubes, between the feeding assembly 5 and the adjacent air guide tubes, and between two adjacent air guide tubes.

下面结合附图描述本申请多个实施例的废气/废液/固废燃烧处理器100及其使用方法。The exhaust gas/waste liquid/solid waste combustion processor 100 according to various embodiments of the present application and the use method thereof will be described below with reference to the accompanying drawings.

实施例1：Example 1:

如图1、图3-图10所示，本申请实施例的燃烧处理器100包括壳体101、调温导风筒2、贴壁导风筒1、助燃导风筒4、煤粉输送导风筒9和供料组件5。As shown in FIG. 1, FIG. 3-FIG. 10, the combustion processor 100 of the embodiment of the present application includes a housing 101, a temperature-adjusting air guide 2, a wall-mounted air guide 1, a combustion-supporting air guide 4, and a pulverized coal conveying guide Air duct 9 and feeding assembly 5.

壳体101具有第一腔102和围成第一腔102的周壁103，第一腔102包括中部的稳燃腔1021、位于稳燃腔1021左侧的导风腔和位于稳燃腔1021右侧的整流腔1022，稳燃腔1021对应的周壁103为锥形面，左端口径小于右端口径，导风腔和整流腔1022为圆筒形，调温导风筒2、贴壁导风筒1、助燃导风筒4、煤粉输送导风筒9设置在导风腔内；The housing 101 has a first cavity 102 and a peripheral wall 103 surrounding the first cavity 102 . The first cavity 102 includes a combustion stabilization chamber 1021 in the middle, an air guide chamber located on the left side of the combustion stabilization chamber 1021 and a combustion stabilization chamber 1021 on the right side. The rectifier cavity 1022 is formed, the peripheral wall 103 corresponding to the combustion stabilization cavity 1021 is a conical surface, the diameter of the left port is smaller than the diameter of the right port, the air guide cavity and the rectifier cavity 1022 are cylindrical, the temperature regulation air guide 2, the wall-mounted air guide 1, The combustion-supporting air guide duct 4 and the pulverized coal conveying air guide duct 9 are arranged in the air guide cavity;

供料组件5包括有机废液输送管53、回流帽52和雾化喷嘴组件，有机废液输送管53与第一腔102同轴设置，有机废液输送管53的进液端位于导风腔内，出液端位于整流腔1022的出口端，回流帽52为一端封闭一端敞开的筒形结构，回流帽52与有机废液输送管53同轴设置，回流帽52位于有机废液输送管53的出液端，敞开端朝向有机废液输送管53的进液端，雾化喷嘴组件包括固定盘54，固定盘54套设在有机废液输送管53的出液端，固定盘54的外圆周面与回流帽52的敞开端连接，在固定盘54上设置有多个贯穿固定盘54的喷射孔541；The feeding assembly 5 includes an organic waste liquid conveying pipe 53, a return cap 52 and an atomizing nozzle assembly. The organic waste liquid conveying pipe 53 is arranged coaxially with the first cavity 102, and the liquid inlet end of the organic waste liquid conveying pipe 53 is located in the air guide cavity. Inside, the liquid outlet end is located at the outlet end of the rectification chamber 1022, the return cap 52 is a cylindrical structure with one end closed and one end open, the return cap 52 is coaxially arranged with the organic waste liquid conveying pipe 53, and the return cap 52 is located in the organic waste liquid conveying pipe 53. The liquid outlet end of the organic waste liquid conveying pipe 53, the open end faces the liquid inlet end of the organic waste liquid conveying pipe 53, the atomizing nozzle assembly includes a fixed disk 54, the fixed disk 54 is sleeved on the liquid outlet end of the organic waste liquid conveying pipe 53, and the outer side of the fixed disk 54 is The circumferential surface is connected with the open end of the return cap 52, and the fixed plate 54 is provided with a plurality of injection holes 541 penetrating the fixed plate 54;

调温导风筒2为圆锥形、椭圆形、圆柱形或者其他任意曲线钝体，调温导风筒2套设在有机废液输送管53的外部且与其同轴设置，调温导风筒2靠近稳燃腔1021一端封闭，该封闭端设置有多个通孔(图中未示出)，远离稳燃腔1021的一端敞开，有机废液输送管53贯穿调温导风筒2靠近稳燃腔1021一端进入稳燃腔1021内，调温导风筒2的内侧面与有机废液输送管53的外侧面之间形成过渡通道31，过渡通道31内设置有点火器(图中未示出)，点火器的火焰穿过通孔后射入第一腔102内，过渡通道内还可以设置火焰检测器(图中未示出)，过渡通道31的最宽直径小于煤粉输送导风筒9的内径，最窄直径大于点火器和/或火焰检测器的最大直径；The temperature-adjusting air guide 2 is a conical, elliptical, cylindrical or other arbitrary curved bluff body. The temperature-adjusting air guide 2 is sleeved on the outside of the organic waste liquid conveying pipe 53 and is arranged coaxially with it. 2. One end close to the combustion stabilization chamber 1021 is closed, and the closed end is provided with a plurality of through holes (not shown in the figure), and the end away from the combustion stabilization chamber 1021 is open. One end of the combustion chamber 1021 enters the stable combustion chamber 1021, and a transition channel 31 is formed between the inner side of the temperature-adjusting air guide duct 2 and the outer side of the organic waste liquid conveying pipe 53, and an igniter (not shown in the figure) is arranged in the transition channel 31. ), the flame of the igniter is injected into the first cavity 102 after passing through the through hole, a flame detector (not shown in the figure) can also be set in the transition channel, and the widest diameter of the transition channel 31 is smaller than the pulverized coal conveying air guide tube 9, the narrowest diameter is greater than the largest diameter of the igniter and/or flame detector;

贴壁导风筒1的外侧面与周壁103的内侧面之间形成贴壁风通道11，贴壁导风筒1包括筒体12和设置在筒体12外侧且沿周向分布的若干个可动定位组件，可动定位组件用于调节贴壁风通道11的截面积，可动定位组件包括套设在筒体12外周面上的柔性部13和调节组件，调节组件包括调节件71和密封垫圈72，在筒体12上沿筒体12的周向间隔设置多个安装孔，安装孔可以为螺纹孔，调节件71可以为调节螺栓，每个螺纹孔对应设置一个调节螺栓，在柔性部13上设置若干个与安装孔对应的光孔，调节螺栓的螺纹端穿过密封垫圈72，柔性部13的光孔，最后旋入筒体12的螺纹孔内进行连接；A wall-adhering air channel 11 is formed between the outer side of the wall-adhering air guide duct 1 and the inner side of the peripheral wall 103 , and the wall-adhering air guide duct 1 includes a cylindrical body 12 and a plurality of adjustable air guides arranged outside the cylindrical body 12 and distributed along the circumferential direction. The movable positioning assembly is used to adjust the cross-sectional area of the air channel 11 attached to the wall. The movable positioning assembly includes the flexible part 13 sleeved on the outer peripheral surface of the cylinder 12 and the adjustment assembly. The adjustment assembly includes the adjustment member 71 and the seal The washer 72 is provided with a plurality of mounting holes on the cylindrical body 12 at intervals along the circumferential direction of the cylindrical body 12. The mounting holes can be threaded holes, and the adjusting member 71 can be an adjusting bolt. Each threaded hole is correspondingly provided with an adjusting bolt. 13 is provided with a number of light holes corresponding to the installation holes, the threaded end of the adjusting bolt passes through the sealing washer 72, the light hole of the flexible part 13, and is finally screwed into the threaded hole of the cylinder body 12 for connection;

助燃导风筒4的外侧面与贴壁导风筒1的内侧面之间形成助燃风通道41；A combustion-supporting air channel 41 is formed between the outer side surface of the combustion-supporting air guide duct 4 and the inner side surface of the wall-mounted air guide duct 1;

煤粉输送导风筒9位于助燃导风筒4和调温导风筒2之间，煤粉输送导风筒9的内外两侧对应两个通道，其中一个可以为煤粉输送通道91，另一可以为调温通道21；The pulverized coal conveying air guide 9 is located between the combustion-supporting air guide 4 and the temperature regulating air guide 2. The inner and outer sides of the pulverized coal conveying air guide 9 correspond to two channels, one of which can be the pulverized coal conveying channel 91, and the other One can be the temperature adjustment channel 21;

在助燃风通道41和调温通道21内可以设置轴向叶轮组件6，调温通道21内置易拆卸的可动轴向叶轮组件6，用于使可燃助燃气体或惰性阻燃气体经过可动轴向叶轮组件6后形成具有切向速度的旋转气流，助燃风通道41可内置易拆卸的可动轴向叶轮组件6，用于使助燃风经过可动轴向叶轮组件6后形成具有切向速度的旋转气流；An axial impeller assembly 6 can be arranged in the combustion-supporting air passage 41 and the temperature-adjusting passage 21, and an easily detachable movable axial impeller assembly 6 is built in the temperature-adjusting passage 21 for allowing the combustible combustion-supporting gas or the inert flame-retardant gas to pass through the movable shaft A rotating airflow with tangential velocity is formed behind the impeller assembly 6, and the combustion-supporting air passage 41 can be built with an easily removable movable axial impeller assembly 6, which is used to make the combustion-supporting air pass through the movable axial impeller assembly 6 to form a tangential velocity. swirling airflow;

煤粉输送通道91可内置易拆卸的浓淡分离结构件(图中未示出)，浓淡分离结构件可分为缩口型、齿轮型和花瓣形，浓淡分离结构件及煤粉输送通道91对应位置上布置有螺纹孔，浓淡分离结构件通过螺栓、密封垫圈72和螺纹孔固定在煤粉输送通道91中。The pulverized coal conveying channel 91 can be built with an easily disassembled concentration separation structure (not shown in the figure). The concentration separation structure can be divided into a constriction type, a gear type and a petal shape. Threaded holes are arranged at the positions, and the concentration separation structure is fixed in the pulverized coal conveying channel 91 through bolts, sealing washers 72 and the threaded holes.

本申请实施例的燃烧处理器100的使用方法，包括以下步骤：The method for using the combustion processor 100 according to the embodiment of the present application includes the following steps:

根据有机废液的热值、废液量及煤种选择合适直径的有机废液输送管53、合适雾化特性的雾化喷嘴组件及浓淡分离组件，如果是挥发分高且热值高的煤种，则浓淡分离组件选择缩口型浓淡分离器或齿轮型浓淡分离器；如果是挥发分低且热值低的煤种，则所述浓淡分离组件选择花瓣形浓淡分离器；According to the calorific value of the organic waste liquid, the amount of waste liquid and the type of coal, select the appropriate diameter of the organic waste liquid conveying pipe 53, the atomization nozzle assembly and the concentration separation assembly with suitable atomization characteristics. If it is coal with high volatile content and high calorific value If it is a coal type with low volatile content and low calorific value, the concentration separation component selects a petal-shaped concentration separator;

分两路通入空气，一路经过助燃风通道41内的可动轴向叶轮组件6后形成具有切向速度的旋转气流直接进入稳燃腔1021，且助燃风通道41与过渡通道31共同作用形成一个嵌套型的高温回流区；另一路通过贴壁风通道11形成贴壁风，贴壁风的一部分形成沿稳燃腔1021壁面流动的冷却空气层，以冷却稳燃腔1021和整流腔1022，使稳燃腔1021和整流腔1022的壁面温度低于40℃，贴壁风的另一部分则与主火焰经整流腔1022形成风包火的高速喷射火焰进入炉膛，由此不仅使燃料稳定燃烧，而且避免了壳体101和炉膛内积灰结焦腐蚀现象的发生；The air is introduced into two paths, one of which passes through the movable axial impeller assembly 6 in the combustion-supporting air passage 41 to form a rotating airflow with a tangential velocity and directly enters the combustion-stabilizing chamber 1021, and the combustion-supporting air passage 41 and the transition passage 31 work together to form A nested high-temperature recirculation zone; the other way forms the wall-adhering wind through the wall-adhering air channel 11, and a part of the wall-adhering wind forms a cooling air layer flowing along the wall of the combustion stabilization chamber 1021 to cool the combustion stabilization chamber 1021 and the rectification chamber 1022 , so that the wall temperature of the combustion stabilization chamber 1021 and the rectification chamber 1022 is lower than 40°C, and the other part of the wall-adhering wind and the main flame through the rectification chamber 1022 form a high-speed jet flame of air-encapsulated fire into the furnace, thereby not only making the fuel burn stably , and avoid the occurrence of fouling and coking corrosion in the shell 101 and the furnace;

贴壁风的风速应比助燃风大，控制在20m/s以上，助燃风和贴壁风的比例优选为1:2，此比例既可以保证燃料稳定燃烧，使助燃风逐层与主火焰混合以降低氮氧化物，也能使贴壁风有足够的动量冷却稳燃腔1021和整流腔1022；The wind speed of the wall-mounted wind should be larger than that of the combustion-supporting wind, and should be controlled above 20m/s. The ratio of the combustion-supporting wind and the wall-mounted wind should preferably be 1:2. This ratio can not only ensure the stable combustion of the fuel, but also allow the combustion-supporting wind to mix with the main flame layer by layer. In order to reduce nitrogen oxides, the wall-mounted wind can also have enough momentum to cool the combustion stabilization chamber 1021 and the rectifier chamber 1022;

与此同时，有机废液经过有机废液输送管53、回流帽52和雾化喷嘴组件组成的回流通道进入高温回流区，其中有机废液输送管53的入口压力需大于有机废液燃烧器内部的压力，控制在0.3～0.5MPa，以防雾化喷嘴堵塞，并且不会导致燃烧处理器100腐蚀，有机废液经过高温回流区预热，根据废液的热值及废液量选择合适的燃烧温度，调温通道21可通入氧化性气体(包括但不限于空气、氧气)、可燃气体(包括但不限于H2、CH4和天然气)以及惰性气体(包括但不限于CO2、N2)，若燃烧区温度较低则通入氧化性气体或可燃气体，温度较高则通入惰性气体，以维持燃烧区温度在700～1600℃之间，煤粉在高温回流区内燃烧，有机废液经过雾化喷嘴组件形成液滴流，并与助燃风及调温气体在过渡通道312的封闭端混合在一起后形成一个多层的主火焰。At the same time, the organic waste liquid enters the high temperature return zone through the return channel composed of the organic waste liquid conveying pipe 53, the return cap 52 and the atomizing nozzle assembly, wherein the inlet pressure of the organic waste liquid conveying pipe 53 needs to be higher than that inside the organic waste liquid burner. The pressure is controlled at 0.3-0.5MPa to prevent the atomization nozzle from being blocked and the combustion processor 100 will not be corroded. Combustion temperature, the temperature adjustment channel 21 can be fed with oxidizing gas (including but not limited to air, oxygen), combustible gas (including but not limited to H2, CH4 and natural gas) and inert gas (including but not limited to CO2, N2), if When the temperature of the combustion zone is low, oxidizing gas or combustible gas is introduced, and when the temperature is high, inert gas is introduced to maintain the temperature of the combustion zone between 700 and 1600 ° C. The pulverized coal is burned in the high temperature return zone, and the organic waste liquid passes through The atomizing nozzle assembly forms a stream of droplets, which are mixed with the combustion air and temperature-adjusting gas at the closed end of the transition channel 312 to form a multi-layered main flame.

本申请由于采取以上技术方案，其具有以下优点：1、本申请以煤粉燃烧处理有机废液，充分利用了有机废液原有热值，通过改变调温通道21内的气体组成和流速，起到调节燃烧区温度的作用，保证燃烧区温度在700～1600℃之间，有效分解废液中的有机物；2、本申请设置了助燃风通道41和贴壁风通道11，可以使空气分成助燃风和贴壁风分别进入燃烧处理器100本体，不仅使空气分级给入燃烧处理器100降低氮氧化物，助燃风与过渡通道31相结合使气液固燃料和空气充分混合稳定燃烧，而且贴壁风可以在稳燃腔1021内形成沿稳燃腔1021壁面流动的冷却空气层，以冷却稳燃腔1021和整流腔1022，使稳燃腔1021和整流腔1022的壁面温度始终低于40℃，不仅可以取消稳燃腔1021的水冷装置，而且避免稳燃腔1021壁面积灰结焦腐蚀现象的发生；3、本申请可以通过可动定位组件调节贴壁风通道11的截面积，进而调整贴壁风的风速，控制助燃风和贴壁风的混合速率，从而控制气液固燃料在燃烧处理器100内的燃烧进程，由此在稳燃腔1021内形成一个内部低氧、高温，外部高氧、低温的环境，这种温度分布和气氛分布，不仅可以达到高燃烧效率和低氮的效果，拓宽燃烧处理器100的负荷调整范围和煤种适应性，而且能有效的解决稳燃室壁面高温腐蚀、积灰及结焦等现象，减少燃烧处理器100的维修频率，延长燃烧处理器100的使用寿命；4、本申请还采用了过渡通道31的设计，该过渡通道31不仅可以内置点火油枪和点火器，而且过渡通道31还可以与内置可动轴向叶轮的助燃风通道41共同作用产生一个高湍流强度的回流区，增强气液固燃料与空气的混合速率，提高燃料在低负荷工况下的燃尽率。The present application has the following advantages due to the adoption of the above technical solutions: 1. The present application uses pulverized coal combustion to process organic waste liquid, fully utilizes the original calorific value of the organic waste liquid, and changes the gas composition and flow rate in the temperature-adjusting channel 21, It plays the role of adjusting the temperature of the combustion zone, ensuring that the temperature of the combustion zone is between 700 and 1600 ° C, and effectively decomposing the organic matter in the waste liquid; 2. The application is provided with a combustion-supporting air channel 41 and a wall-mounted air channel 11, which can make the air into The combustion-supporting wind and the wall-adhering wind enter the body of the combustion processor 100 respectively, which not only makes the air graded into the combustion processor 100 to reduce nitrogen oxides, but also combines the combustion-supporting air with the transition channel 31 to make the gas-liquid-solid fuel and air fully mix and stably burn, but also The wall-adhering wind can form a cooling air layer in the combustion stabilization chamber 1021 that flows along the wall of the combustion stabilization chamber 1021 to cool the combustion stabilization chamber 1021 and the rectification chamber 1022, so that the wall temperature of the combustion stabilization chamber 1021 and the rectification chamber 1022 is always lower than 40 ℃, not only can the water cooling device of the combustion stabilization chamber 1021 be eliminated, but also avoid the occurrence of ash coking and corrosion in the wall area of the combustion stabilization chamber 1021; 3. The application can adjust the cross-sectional area of the wall-mounted air channel 11 through the movable positioning component, and then adjust the The wind speed of the wall-adhering wind controls the mixing rate of the combustion-supporting wind and the wall-adhering wind, thereby controlling the combustion process of the gas-liquid-solid fuel in the combustion processor 100, thereby forming an internal low-oxygen, high-temperature, external In the high oxygen and low temperature environment, this temperature distribution and atmosphere distribution can not only achieve the effect of high combustion efficiency and low nitrogen, widen the load adjustment range and coal type adaptability of the combustion processor 100, but also can effectively solve the problem of stable combustion chamber. The phenomenon of high temperature corrosion, ash accumulation and coking on the wall surface reduces the maintenance frequency of the combustion processor 100 and prolongs the service life of the combustion processor 100; 4. The application also adopts the design of the transition channel 31, and the transition channel 31 can not only have built-in ignition The oil gun and igniter, and the transition channel 31 can also work together with the combustion-supporting air channel 41 with the built-in movable axial impeller to generate a high turbulence intensity return area, enhance the mixing rate of gas-liquid-solid fuel and air, and improve the fuel at low temperature. Burnout rate under load conditions.

实施例2：Example 2:

如图1-图8所示，根据本申请实施例的燃烧处理器100包括壳体101、贴壁导风筒1、调温导风筒2、废气输送导风筒3和供料组件5。壳体101具有第一腔102和围成第一腔102的周壁103。As shown in FIGS. 1-8 , a combustion processor 100 according to an embodiment of the present application includes a housing 101 , a wall-mounted air guide 1 , a temperature adjustment air guide 2 , an exhaust gas conveying air guide 3 and a feeding assembly 5 . The housing 101 has a first cavity 102 and a peripheral wall 103 surrounding the first cavity 102 .

贴壁导风筒1设在第一腔102内，贴壁导风筒1的外周面和周壁103之间形成贴壁风通道11，调温导风筒2设在第一腔102内，调温导风筒2的外周面与贴壁导风筒1的内周面之间形成调温通道21，供料组件5设在第一腔102内，废气输送导风筒3设在第一腔102内，废气输送导风筒3套设在供料组件5上，废气输送导风筒3的内周面与供料组件5的外周面之间形成过渡通道31，废气输送导风筒3的外周面与调温导风筒2的内周面之间形成废气通道32。The wall-adhering air duct 1 is arranged in the first cavity 102, and a wall-adhering air channel 11 is formed between the outer peripheral surface of the wall-adhering air duct 1 and the peripheral wall 103, and the temperature-adjusting air duct 2 is arranged in the first cavity 102. A temperature adjustment channel 21 is formed between the outer peripheral surface of the warm air guide duct 2 and the inner peripheral surface of the wall-mounted air guide duct 1 , the feeding assembly 5 is arranged in the first cavity 102 , and the exhaust gas conveying air guide duct 3 is arranged in the first cavity In 102, the exhaust gas conveying air guide tube 3 is sleeved on the feeding assembly 5, and a transition channel 31 is formed between the inner peripheral surface of the exhaust gas conveying air guide tube 3 and the outer peripheral surface of the feeding assembly 5. An exhaust gas passage 32 is formed between the outer peripheral surface and the inner peripheral surface of the temperature-adjusting air guide duct 2 .

具体地，如图1-图3所示，壳体101的左端和右端大体为圆柱形，壳体101的中间段大体为圆锥形，贴壁导风筒1、调温导风筒2、废气输送导风筒3和供料组件5均设在第一腔102内。Specifically, as shown in FIGS. 1-3 , the left and right ends of the casing 101 are generally cylindrical, the middle section of the casing 101 is generally conical, the wall-mounted air guide 1, the temperature-adjusted air guide 2, the exhaust gas Both the conveying air guide tube 3 and the feeding assembly 5 are arranged in the first cavity 102 .

其中，供料组件5沿左右方向水平设置，且供料组件5的轴线和第一腔102的轴线大体重合，即供料组件5位于第一腔102的中间位置，由此，可使得煤粉通过供料组件5进入第一腔102后也处在第一腔102的中间位置，使得煤粉燃烧更充分，有利于提高煤粉的利用率。Wherein, the feeding assembly 5 is arranged horizontally along the left-right direction, and the axis of the feeding assembly 5 and the axis of the first cavity 102 are substantially coincident, that is, the feeding assembly 5 is located in the middle position of the first cavity 102, so that the pulverized coal can be made After entering the first cavity 102 through the feeding component 5, it is also in the middle position of the first cavity 102, so that the pulverized coal is burned more fully, which is beneficial to improve the utilization rate of the pulverized coal.

贴壁导风筒1、调温导风筒2、废气输送导风筒3均设在壳体101的左端的内侧，其中，废气输送导风筒3套设在供料组件5的左端上，调温导风筒2套设在废气输送导风筒3上，贴壁导风筒1套设在调温导风筒2上，且在第一腔102的轴向方向上，贴壁导风筒1的右端、调温导风筒2的右端和废气输送导风筒3的右端大体对齐。由此，使得从贴壁风通道11中通入第一腔102内的空气、从调温通道21中通入第一腔102内的调温气体和从废气通道32中通入第一腔102内的废气在进入第一腔102时不会相互干扰，使得上述调温气体和废气能够更好地流向第一腔102的内部，有利于调温气体和废气充分燃烧，提高了废气处理的效率。The wall-mounted air guide 1, the temperature adjustment air guide 2, and the exhaust gas conveying air guide 3 are all arranged on the inner side of the left end of the housing 101, wherein the exhaust gas conveying air guide 3 is sleeved on the left end of the feeding assembly 5, The temperature-adjusting air guide 2 is sleeved on the exhaust gas conveying air guide 3, and the wall-mounted air guide 1 is sleeved on the temperature-adjusting air guide 2, and in the axial direction of the first cavity 102, the wall-mounted air guide The right end of the tube 1 , the right end of the temperature regulating air guide tube 2 and the right end of the exhaust gas conveying air guide tube 3 are generally aligned. In this way, the air passing into the first cavity 102 from the wall-mounted air channel 11 , the temperature regulating gas passing into the first cavity 102 from the temperature regulating channel 21 , and the first cavity 102 passing from the exhaust gas channel 32 The exhaust gas inside will not interfere with each other when entering the first chamber 102, so that the above-mentioned temperature-adjusting gas and exhaust gas can flow to the inside of the first chamber 102 better, which is conducive to the full combustion of the temperature-adjusting gas and exhaust gas, and improves the efficiency of exhaust gas treatment .

同时，上述空气更好地流向第一腔102的内部，有利于提高空气对周壁103的冷却效果，该空气会沿着周壁103流动以形成空气冷却层，该空气冷却层可很好的降低周壁103的温度，使周壁103的温度保持稳定，避免了周壁103表面积灰结焦和腐蚀现象的发生，有利于延长燃烧处理器100的使用寿命。At the same time, the above-mentioned air flows better to the inside of the first cavity 102, which is beneficial to improve the cooling effect of the air on the peripheral wall 103. The air will flow along the peripheral wall 103 to form an air cooling layer, which can effectively reduce the peripheral wall. The temperature of the peripheral wall 103 keeps the temperature of the peripheral wall 103 stable, avoids the occurrence of coking and corrosion on the surface of the peripheral wall 103 , and is beneficial to prolong the service life of the combustion processor 100 .

由此，本申请实施例的燃烧处理器100具有废气燃烧充分和周壁103冷却效果好等优点。Therefore, the combustion processor 100 of the embodiment of the present application has the advantages of sufficient combustion of exhaust gas and good cooling effect of the peripheral wall 103 .

在一些实施例中，如图2-图3所示，燃烧处理器100进一步包括助燃导风筒4，助燃导风筒4设在第一腔102内，助燃导风筒4在内外方向上位于贴壁导风筒1和调温导风筒2之间。助燃导风筒4的外周面和贴壁导风筒1的内周面之间形成助燃风通道41，助燃导风筒4的内周面和调温导风筒2的外周面之间形成调温通道21。In some embodiments, as shown in FIGS. 2-3 , the combustion processor 100 further includes a combustion-supporting air guide 4, which is arranged in the first cavity 102, and the combustion-supporting air guide 4 is located in the inner and outer directions. Between the wall-mounted air duct 1 and the temperature-adjusted air duct 2. A combustion-supporting air channel 41 is formed between the outer peripheral surface of the combustion-supporting air guide duct 4 and the inner peripheral surface of the wall-adhering air guide duct 1 , and a regulating air channel 41 is formed between the inner peripheral surface of the combustion-supporting air guide duct 4 and the outer peripheral surface of the temperature-adjusting air guide duct 2 . Warm channel 21.

具体地，如图2和图3所示，在贴壁导风筒1和调温导风筒2之间添加助燃导风筒4，可将贴壁导风筒1和调温导风筒2之间原有的调温通道21进一步分隔成助燃风通道41和调温通道21。可将空气从助燃风通道41通入第一腔102内，该空气与调温气体混合，有利于提高第一腔102内煤粉的燃烧效率，使得第一腔102内的燃烧更稳定，废气的燃烧效果更好。Specifically, as shown in FIGS. 2 and 3 , a combustion-supporting air duct 4 is added between the wall-mounted air duct 1 and the temperature-adjusting air duct 2, so that the wall-adhering air duct 1 and the temperature-adjusting air duct 2 can be connected to each other. The original temperature adjustment channel 21 is further divided into a combustion-supporting air channel 41 and a temperature adjustment channel 21 . Air can be introduced into the first cavity 102 from the combustion-supporting air passage 41, and the air is mixed with the temperature-adjusting gas, which is beneficial to improve the combustion efficiency of pulverized coal in the first cavity 102, so that the combustion in the first cavity 102 is more stable, and the exhaust gas The burning effect is better.

可以理解的是，上述调温气体包括氧化性气体、可燃气体和惰性气体中的一种或多种。It can be understood that the above temperature-adjusting gas includes one or more of oxidizing gas, combustible gas and inert gas.

本申请实施例中的调温气体用于调节第一腔102内的燃烧温度，即当第一腔102内的燃烧温度高于预设值时，可向第一腔102内冲入惰性气体，该惰性气体用于抑制第一腔102内的燃烧程度，以降低第一腔102内的燃烧温度。其中，惰性气体包括CO ₂、N ₂和其它惰性气体中的一种或多种。 The temperature-adjusting gas in the embodiment of the present application is used to adjust the combustion temperature in the first cavity 102, that is, when the combustion temperature in the first cavity 102 is higher than a preset value, an inert gas can be injected into the first cavity 102, The inert gas is used to suppress the degree of combustion in the first chamber 102 to reduce the combustion temperature in the first chamber 102 . Wherein, the inert gas includes one or more of CO ₂ , N ₂ and other inert gases.

当第一腔102内的燃烧温度低于预设值时，可向第一腔102内冲入氧化性气体和/或可燃气体，有利于提高第一腔102内的燃烧温度。其中，氧化性气体包括空气、氧气，可燃气体包括H ₂、CH ₄和天然气。 When the combustion temperature in the first cavity 102 is lower than the preset value, oxidizing gas and/or combustible gas may be injected into the first cavity 102 , which is beneficial to increase the combustion temperature in the first cavity 102 . The oxidizing gas includes air and oxygen, and the combustible gas includes H ₂ , CH ₄ and natural gas.

优选地，本申请实施例的燃烧处理器100内的燃烧区温度控制在700-1600℃之间，在该温度范围内，可充分燃烧含氟化物的废气。Preferably, the temperature of the combustion zone in the combustion processor 100 of the embodiment of the present application is controlled between 700-1600° C., within this temperature range, the exhaust gas containing fluoride can be fully combusted.

在一些实施例中，如图3所示，供料组件5包括煤粉管51和回流帽52。煤粉管51沿第一腔102的轴线设在第一腔102内，煤粉管51具有入口端(例如图3中煤粉管51的左端)和出口端(例如图3中煤粉管51的右端)。废气输送导风筒3套设在煤粉管51的入口端处，回流帽52设在煤粉管51的出口端，回流帽52大体为筒形，回流帽52的出口朝向煤粉管51的入口端。In some embodiments, as shown in FIG. 3 , the feed assembly 5 includes a pulverized coal pipe 51 and a return cap 52 . The pulverized coal pipe 51 is arranged in the first cavity 102 along the axis of the first cavity 102, and the pulverized coal pipe 51 has an inlet end (for example, the left end of the pulverized coal pipe 51 in FIG. 3 ) and an outlet end (for example, the pulverized coal pipe 51 in FIG. 3 ) right end). The exhaust gas conveying air guide tube 3 is sleeved at the inlet end of the pulverized coal pipe 51, and the return cap 52 is arranged at the outlet end of the pulverized coal pipe 51. entry port.

具体地，如图3所示，煤粉管51为直管形结构，煤粉在气流的带动下从煤粉管51的左端进入煤粉管51，煤粉在煤粉管51内向右移动。回流帽52设在煤粉管51的右端处，回流帽52的左端撇开、右端封闭，煤粉从煤粉管51的右端冲出后会撞击在回流帽52的右端上，反射后的煤粉从回流帽52的左端冲出并流向第一腔102的内部。Specifically, as shown in FIG. 3 , the pulverized coal pipe 51 has a straight tubular structure. The pulverized coal enters the pulverized coal pipe 51 from the left end of the pulverized coal pipe 51 driven by the airflow, and the pulverized coal moves to the right in the pulverized coal pipe 51 . The return cap 52 is arranged at the right end of the pulverized coal pipe 51. The left end of the return cap 52 is left open and the right end is closed. It is punched out from the left end of the return cap 52 and flows into the interior of the first cavity 102 .

其中，煤粉先撞击在回流帽52的右端上，再反射到第一腔102内，使得煤粉的粒径更小、煤粉更细化，有利于提高煤粉的燃烧效率。同时，经过反射后的煤粉会弥散在第一腔102内，也使得煤粉与废气的接触更充分，有利于废气的充分燃烧。The pulverized coal first hits the right end of the return cap 52 and is then reflected into the first cavity 102, so that the particle size of the pulverized coal is smaller and the pulverized coal is more refined, which is beneficial to improve the combustion efficiency of the pulverized coal. At the same time, the reflected pulverized coal will be dispersed in the first cavity 102, which also makes the contact between the pulverized coal and the exhaust gas more sufficient, which is conducive to the full combustion of the exhaust gas.

在一些实施例中，如图4所示，燃烧处理器100进一步包括叶轮组件6，助燃风通道41、调温通道21和废气通道32内均设有叶轮组件6，叶轮组件6包括彼此相连的叶片61和伸缩杆62，伸缩杆62沿第一腔102的轴向设置。In some embodiments, as shown in FIG. 4 , the combustion processor 100 further includes an impeller assembly 6 . The combustion air passage 41 , the temperature adjustment passage 21 and the exhaust gas passage 32 are all provided with an impeller assembly 6 , and the impeller assembly 6 includes an impeller assembly 6 connected to each other. The blade 61 and the telescopic rod 62 are arranged along the axial direction of the first cavity 102 .

具体地，如图4所示，伸缩杆62可沿第一腔102的轴线设在上述气体通道内，伸缩杆62的左端可与构成上述通道的导风筒相连，伸缩杆62的右端设有叶片61，叶片61可自由旋转，上述通道内的气体在进入第一腔102内时会流经叶片61，叶片61使得流经叶片61的气体发生旋转并流向第一腔102的中心位置。由此，使得助燃气体、调温气体和废气之间的混合更充分，有利于提高废气的处理效果。Specifically, as shown in FIG. 4 , the telescopic rod 62 can be arranged in the above-mentioned gas channel along the axis of the first cavity 102 , the left end of the telescopic rod 62 can be connected with the air guide tube constituting the above-mentioned channel, and the right end of the telescopic rod 62 is provided with The vane 61, the vane 61 can rotate freely, the gas in the above-mentioned passage will flow through the vane 61 when entering the first cavity 102, and the vane 61 makes the gas flowing through the vane 61 rotate and flow to the center of the first cavity 102. Thereby, the mixing between the combustion-supporting gas, the temperature-adjusting gas and the exhaust gas is more sufficient, which is beneficial to improve the treatment effect of the exhaust gas.

在一些实施例中，如图5所示，贴壁导风筒1包括筒体12和套设在筒体12的外周面上的柔性部13。In some embodiments, as shown in FIG. 5 , the wall-mounted air guide tube 1 includes a cylindrical body 12 and a flexible portion 13 sleeved on the outer peripheral surface of the cylindrical body 12 .

燃烧处理器100进一步包括调节组件7，调节组件7包括调节件71和密封垫圈72，筒体12上设有安装孔14，调节件71的第一部分穿过柔性部13且设在安装孔14内，调节件71的第二部分压制在柔性部13的外周面上，密封垫圈72设在调节件71的第二部分和柔性部13的外周面之间。The combustion processor 100 further includes an adjustment assembly 7 , the adjustment assembly 7 includes an adjustment member 71 and a sealing gasket 72 , a mounting hole 14 is provided on the cylindrical body 12 , and the first part of the adjustment member 71 passes through the flexible portion 13 and is disposed in the mounting hole 14 , the second part of the adjustment member 71 is pressed on the outer peripheral surface of the flexible part 13 , and the sealing gasket 72 is provided between the second part of the adjustment member 71 and the outer peripheral surface of the flexible part 13 .

具体地，如图5所示，调节件71可以为螺栓，调节件71的第一部分为螺栓的螺纹部，调节件71的第二部分为螺帽部。柔性部13的内周面和筒体12的外周面相连，安装孔14为螺纹孔，调节件71的螺纹部设在安装孔14内，通过拧紧调节件71可使调节件71的螺帽部压紧柔性部13，使得柔性部13的外径缩小(体积缩小)，由此，扩大了柔性部13的外周面和周壁103之间的间隙，即扩大了贴壁风通道11的流通面积。Specifically, as shown in FIG. 5 , the adjusting member 71 may be a bolt, the first part of the adjusting member 71 is the threaded part of the bolt, and the second part of the adjusting member 71 is the nut part. The inner peripheral surface of the flexible portion 13 is connected with the outer peripheral surface of the cylinder body 12 , the mounting hole 14 is a threaded hole, and the threaded portion of the adjusting member 71 is set in the mounting hole 14 , and the nut portion of the adjusting member 71 can be adjusted by tightening the adjusting member 71 . The flexible portion 13 is compressed to reduce the outer diameter (volume reduction) of the flexible portion 13 , thereby expanding the gap between the outer peripheral surface of the flexible portion 13 and the peripheral wall 103 , that is, expanding the flow area of the adhering air passage 11 .

其中，密封垫圈72设在调节件71的螺帽部和柔性部13之间，密封垫圈72可用于密封安装孔14，使得贴壁风通道11与助燃风通道41之间不发生气体交换，有利于提高燃烧处理器100的密封性。同时，调节件71为刚性材料，密封垫圈72避免了调节件71直接压紧在柔性部13上，防止调节件71刮伤柔性部13，有利于延长柔性部13的使用寿命。The sealing washer 72 is provided between the nut part and the flexible part 13 of the adjusting member 71. The sealing washer 72 can be used to seal the mounting hole 14, so that no gas exchange occurs between the wall-mounted air passage 11 and the combustion-supporting air passage 41. It is beneficial to improve the sealing performance of the combustion processor 100 . Meanwhile, the adjusting member 71 is a rigid material, and the sealing gasket 72 prevents the adjusting member 71 from being directly pressed on the flexible portion 13 , prevents the adjusting member 71 from scratching the flexible portion 13 , and is beneficial to prolong the service life of the flexible portion 13 .

在一些实施例中，如图6-图8所示，燃烧处理器100进一步包括煤粉分离器8，煤粉分离器8设在煤粉管51的入口端，煤粉分离器8为喉口形分离器81、齿轮形分离器82或花瓣形分离器83。In some embodiments, as shown in FIGS. 6-8 , the combustion processor 100 further includes a pulverized coal separator 8 , which is arranged at the inlet end of the pulverized coal pipe 51 , and the pulverized coal separator 8 is throat-shaped. Separator 81 , gear-shaped separator 82 or petal-shaped separator 83 .

可以理解的是，本申请实施例的燃烧处理器100可根据不同的煤粉种类选择不同的煤粉分离器8。优选地，如果是挥发分高且热值高的煤种，则选择喉口形分离器81或齿轮形分离器82中的一种。如果是挥发分低且热值低的煤种，则选择花瓣形分离器83。It can be understood that, the combustion processor 100 in the embodiment of the present application can select different pulverized coal separators 8 according to different types of pulverized coal. Preferably, if it is coal with high volatile content and high calorific value, one of the throat-shaped separator 81 or the gear-shaped separator 82 is selected. If it is coal with low volatile content and low calorific value, the petal-shaped separator 83 is selected.

在一些实施例中，如图3所示，废气输送导风筒3具有沿煤粉管51的轴向相对设置的第一端(例如图3中废气输送导风筒3的左端)和第二端(例如图3中废气输送导风筒3的右端)。废气输送导风筒3的第一端敞开，废气输送导风筒3的第二端上设有多个通孔(未示出)。燃烧处理器100进一步包括火焰检测器(未示出)和点火器(未示出)，火焰检测器和点火器设在废气输送导风筒3内，点火器的火焰穿过通孔后射入第一腔102内。In some embodiments, as shown in FIG. 3 , the exhaust gas conveying air duct 3 has a first end (for example, the left end of the exhaust gas conveying air duct 3 in FIG. 3 ) and a second oppositely disposed along the axial direction of the pulverized coal pipe 51 . end (for example, the right end of the exhaust gas conveying air guide tube 3 in FIG. 3 ). The first end of the exhaust gas conveying air guide tube 3 is open, and the second end of the exhaust gas conveying air guide tube 3 is provided with a plurality of through holes (not shown). The combustion processor 100 further includes a flame detector (not shown) and an igniter (not shown), the flame detector and the igniter are arranged in the exhaust gas conveying air guide 3, and the flame of the igniter is injected into the through hole after passing through. inside the first cavity 102 .

具体地，如图3所示，废气输送导风筒3大体为桶形，废气输送导风筒3的右端为圆板形结构，废气输送导风筒3的右端朝向第一腔102的内部，火焰检测器和点火器设在煤粉管51的外周面和废气输送导风筒3的内周面之间，其中，点火器用于点燃第一腔102内的煤粉和废气，火焰检测器用于检测煤粉管51的外周面和废气输送导风筒3的内周面之间是否存在火焰，有利于提高燃烧处理器100的安全性。Specifically, as shown in FIG. 3 , the exhaust gas conveying air guide tube 3 is generally barrel-shaped, the right end of the exhaust gas conveying air guide tube 3 is a disc-shaped structure, and the right end of the exhaust gas conveying air guide tube 3 faces the interior of the first cavity 102 , The flame detector and the igniter are arranged between the outer peripheral surface of the pulverized coal pipe 51 and the inner peripheral surface of the exhaust gas conveying air duct 3, wherein the igniter is used to ignite the pulverized coal and exhaust gas in the first chamber 102, and the flame detector is used to ignite the pulverized coal and exhaust gas in the first chamber 102. Detecting whether there is a flame between the outer peripheral surface of the pulverized coal pipe 51 and the inner peripheral surface of the exhaust gas conveying air guide duct 3 is beneficial to improve the safety of the combustion processor 100 .

本申请实施例的燃烧处理器100的使用方法包括以下步骤：The method for using the combustion processor 100 according to the embodiment of the present application includes the following steps:

根据废气的热值、气量和所选用的煤种确定燃烧处理器100内的燃烧温度，优选地，在处理含氟化物的废气时，控制第一腔102内102的燃烧温度在700-1600℃之间。The combustion temperature in the combustion processor 100 is determined according to the calorific value of the exhaust gas, the amount of gas and the selected coal type. Preferably, when the exhaust gas containing fluoride is treated, the combustion temperature of the first chamber 102 is controlled to be 700-1600° C. between.

废气通过废气通道32进入燃烧处理器100内，煤粉经过供料组件5进入燃烧处理器100内。The exhaust gas enters the combustion processor 100 through the exhaust gas passage 32 , and the pulverized coal enters the combustion processor 100 through the feeding assembly 5 .

空气分成两路进入燃烧处理器100内，其中，一路空气通过助燃风通道41进入燃烧处理器100内，另一炉空气通过贴壁风通道11进入燃烧处理器100内并形成贴壁风，贴壁风的至少一部分沿燃烧处理器100的周壁103流动形成冷却层，点燃燃烧处理器100内的煤粉和废气。The air enters into the combustion processor 100 in two ways, one of which enters the combustion processor 100 through the combustion-supporting air channel 41, and the other furnace air enters the combustion processor 100 through the wall-mounted air channel 11 and forms a wall-mounted wind. At least a part of the wall wind flows along the peripheral wall 103 of the combustion processor 100 to form a cooling layer, and ignite the pulverized coal and exhaust gas in the combustion processor 100 .

在一些实施例中，当燃烧处理器100的周壁103的温度高于预设温度时，压缩贴壁导风筒1的柔性部以扩大贴壁风通道11的流通面积，可选地，预设温度为40℃。当周壁103的温度高于40℃时，可扩大贴壁风通道11的流通面积，增大空气的流量，有利于更快的降低周壁103的温度。In some embodiments, when the temperature of the peripheral wall 103 of the combustion processor 100 is higher than a preset temperature, the flexible part of the wall-mounted air guide duct 1 is compressed to expand the flow area of the wall-mounted air passage 11 , optionally, a predetermined temperature The temperature was 40°C. When the temperature of the peripheral wall 103 is higher than 40° C., the flow area of the wall-mounted air passage 11 can be expanded, and the air flow rate can be increased, which is beneficial to reduce the temperature of the peripheral wall 103 more quickly.

在一些实施例中，根据煤粉的煤种选用对应的煤粉分离器8，煤粉分离器8为喉口形分离器81、齿轮形分离器82或花瓣形分离器83，可选地，废气为含有氟化物的废气。In some embodiments, the corresponding pulverized coal separator 8 is selected according to the coal type of pulverized coal, and the pulverized coal separator 8 is a throat-shaped separator 81, a gear-shaped separator 82 or a petal-shaped separator 83. For the exhaust gas containing fluoride.

实施例3：Example 3:

如图3-图8、图12和图13所示，根据本申请实施例的燃烧处理器100燃烧处理器100包括壳体101、贴壁导风筒1、助燃导风筒2、供料组件5和调温导风筒3。As shown in FIGS. 3-8 , 12 and 13 , the combustion processor 100 according to the embodiment of the present application includes a casing 101 , a wall-mounted air guide 1 , a combustion-supporting air guide 2 , and a feeding assembly 5 and the temperature-adjusting air duct 3.

壳体101具有第一腔102和围成第一腔102的周壁103。贴壁导风筒1设在第一腔102内，贴壁导风筒1的外周面和周壁103之间形成贴壁风通道11。助燃导风筒2设在第一腔102内，助燃导风筒2的外周面与贴壁导风筒1的内周面之间形成助燃风通道21。供料组件5设在第一腔102内，调温导风筒3设在第一腔102内，调温导风筒3套设在供料组件5上，调温导风筒3的内周面与供料组件5的外周面之间形成过渡通道31，调温导风筒3的外周面与助燃导风筒2的内周面之间形成调温通道32。The housing 101 has a first cavity 102 and a peripheral wall 103 surrounding the first cavity 102 . The wall-adhering air guide tube 1 is arranged in the first cavity 102 , and a wall-adhering air channel 11 is formed between the outer peripheral surface of the wall-adhering air guide tube 1 and the peripheral wall 103 . The combustion-supporting air guide 2 is arranged in the first cavity 102 , and a combustion-supporting air channel 21 is formed between the outer peripheral surface of the combustion-supporting air guide 2 and the inner peripheral surface of the wall-adhering air guide 1 . The feeding component 5 is set in the first cavity 102, the temperature regulating air guide tube 3 is set in the first cavity 102, the temperature regulating air guiding tube 3 is sleeved on the feeding component 5, and the inner circumference of the temperature regulating air guiding tube 3 is set in the first cavity 102. A transition channel 31 is formed between the surface and the outer peripheral surface of the feed assembly 5 , and a temperature regulation channel 32 is formed between the outer peripheral surface of the temperature-adjusting air guide duct 3 and the inner peripheral surface of the combustion-supporting air guide duct 2 .

根据本申请实施例的利用燃烧处理器100的使用方法包括以下步骤：The method for using the combustion processor 100 according to the embodiment of the present application includes the following steps:

根据垃圾焚灰的成分确定燃烧处理器100的燃烧温度，垃圾焚灰和煤粉通过煤粉供应组,5进入燃烧处理器100内，空气分成两路进入燃烧处理器100内，其中，一路空气通过助燃风通道21进入燃烧处理器100内，另一炉空气通过贴壁风通道11进入燃烧处理器100内并形成贴壁风，贴壁风的至少一部分沿燃烧处理器100的周壁103流动形成冷却层，点燃燃烧处理器100内的煤粉和垃圾焚灰。The combustion temperature of the combustion processor 100 is determined according to the composition of the garbage incineration ash. The garbage incineration ash and pulverized coal enter the combustion processor 100 through the pulverized coal supply group 5, and the air enters the combustion processor 100 in two ways. The other furnace air enters the combustion processor 100 through the combustion-supporting air passage 21 , and another furnace air enters the combustion processor 100 through the wall-adhering air passage 11 to form a wall-adhering wind. At least a part of the wall-adhering wind flows along the peripheral wall 103 of the combustion processor 100 to form The cooling layer ignites the coal powder and garbage incineration ash in the combustion processor 100 .

具体地，如图1-图2所示，供料组件5沿左右方向水平设置，且供料组件5的轴线和第一腔102的轴线大体重合，即供料组件5位于第一腔102的中间位置。煤粉和垃圾焚灰均通过供料组件5的左端进入供料组件5内，并通过供料组件5的右端进入第一腔102内，由此，可使得煤粉和垃圾焚灰通过供料组件5进入第一腔102后也处在第一腔102的中间位置，使得煤粉和垃圾焚灰燃烧更充分，有利于提高煤粉的利用率，提高垃圾焚灰的分解率。Specifically, as shown in FIGS. 1-2 , the feeding assembly 5 is arranged horizontally along the left-right direction, and the axis of the feeding assembly 5 and the axis of the first cavity 102 are substantially coincident, that is, the feeding assembly 5 is located at the side of the first cavity 102 . in the middle. Both the pulverized coal and the garbage incineration ash enter the feeding assembly 5 through the left end of the feeding assembly 5, and enter the first cavity 102 through the right end of the feeding assembly 5, so that the pulverized coal and the garbage incineration ash can pass through the feeding After the assembly 5 enters the first cavity 102, it is also in the middle position of the first cavity 102, so that the pulverized coal and the garbage incineration ash are burned more fully, which is beneficial to improve the utilization rate of the pulverized coal and the decomposition rate of the garbage incineration ash.

贴壁导风筒1、助燃导风筒2、调温导风筒3均设在壳体101的左端的内侧，其中，调温导风筒3套设在供料组件5的左端上，助燃导风筒2套设在调温导风筒3上，贴壁导风筒1套设在助燃导风筒2上，且在第一腔102的轴向方向上，贴壁导风筒1的右端、助燃导风筒2的右端和调温导风筒3的右端大体对齐。由此，使得从贴壁风通道11中通入第一腔102内的空气和从调温通道32中通入第一腔102内的废气在进入第一腔102时不会相互干扰，使得上述调温气体能够更好地流向第一腔102的内部，有利于提高调温气体的利用率。The wall-mounted air guide 1, the combustion-supporting air guide 2, and the temperature-adjusting air guide 3 are all arranged on the inner side of the left end of the housing 101, wherein the temperature-adjusting air guide 3 is sleeved on the left end of the feed assembly 5 to support combustion. The air guide duct 2 is sleeved on the temperature-adjusting air guide duct 3, the wall-mounted air guide duct 1 is sleeved on the combustion-supporting air guide duct 2, and in the axial direction of the first cavity 102, the wall-mounted air guide duct 1 is sleeved. The right end, the right end of the combustion-supporting air guide duct 2 and the right end of the temperature-adjusting air guide duct 3 are generally aligned. Therefore, the air passing into the first cavity 102 from the wall-mounted air channel 11 and the exhaust gas passing into the first cavity 102 from the temperature adjustment channel 32 will not interfere with each other when entering the first cavity 102, so that the above-mentioned The temperature-adjusting gas can flow to the inside of the first cavity 102 better, which is beneficial to improve the utilization rate of the temperature-adjusting gas.

由此，本申请实施例的利用燃烧处理器100实施的垃圾焚灰处理方法具有垃圾焚灰的分解率高和周壁103冷却效果好等优点。Therefore, the waste incineration ash treatment method implemented by the combustion processor 100 in the embodiment of the present application has the advantages of high decomposition rate of the waste incineration ash and good cooling effect of the peripheral wall 103 .

在一些实施例中，在使垃圾焚灰和煤粉进入燃烧处理器100内之前，将不可燃粉体掺混物、煤粉和垃圾焚灰混合以便利用不可燃粉体掺混物吸附垃圾焚灰熔融后的重金属元素。In some embodiments, the non-combustible powder blend, coal powder, and waste incineration ash are mixed to adsorb the waste incineration with the non-combustible powder blend before passing the waste incineration ash and coal powder into the combustion processor 100 . Heavy metal elements after ash melting.

可以理解的是，不可燃粉体掺混物主要成分为硅化物，不可燃粉体掺混物在燃烧处理器100内会逐渐熔融，熔融后的氧化硅会与垃圾焚灰中分解出的重金属元素相遇，氧化硅可有效地包裹重金属元素，减少了重金属元素的排放，提高了垃圾焚灰的无害化处理的程度。It can be understood that the main component of the non-combustible powder admixture is silicide, the non-combustible powder admixture will gradually melt in the combustion processor 100, and the melted silicon oxide will be combined with the heavy metals decomposed from the waste incineration ash. When elements meet, silicon oxide can effectively wrap heavy metal elements, reduce the discharge of heavy metal elements, and improve the degree of harmless treatment of waste incineration ash.

在一些实施例中，利用燃烧处理器100实施的垃圾焚灰处理方法进一步包括混合装置(未示出)。混合装置用于混合垃圾焚灰与煤粉和/或垃圾焚灰、煤粉与不可燃粉体掺混物。由此，可在通入燃烧处理器100前将垃圾焚灰与煤粉和/或垃圾焚灰、煤粉与不可燃粉体掺混物混合均匀，有利于提高煤粉的燃烧效率和不可燃粉体掺混物包裹重金属元素的效率。In some embodiments, the waste incineration ash treatment method implemented using the combustion processor 100 further includes a mixing device (not shown). The mixing device is used to mix waste incineration ash and coal powder and/or waste incineration ash, coal powder and non-combustible powder. Thereby, the waste incineration ash and coal powder and/or the mixture of waste incineration ash, coal powder and non-combustible powder can be uniformly mixed before passing into the combustion processor 100, which is beneficial to improve the combustion efficiency and non-combustibility of coal powder. Encapsulation efficiency of heavy metal elements in powder blends.

在一些实施例中。垃圾焚灰的质量占垃圾焚灰与煤粉的总质量的20％-80％，垃圾焚灰的质量占垃圾焚灰、煤粉与不可燃粉体掺混物的总质量的20％-80％。由此，可将垃圾焚灰充分燃烧。In some embodiments. The mass of waste incineration ash accounts for 20%-80% of the total mass of waste incineration ash and coal powder, and the mass of waste incineration ash accounts for 20%-80% of the total mass of the mixture of waste incineration ash, coal powder and non-combustible powder. %. Thereby, the refuse incineration ashes can be sufficiently burned.

当垃圾焚灰的质量占比为20％时，垃圾焚灰的分解效果最好，但成本较高。When the mass ratio of waste incineration ash is 20%, the decomposition effect of waste incineration ash is the best, but the cost is higher.

当垃圾焚灰的质量占比为80％时，垃圾焚灰的分解效果相对较差，但成本大幅度降低。When the mass proportion of waste incineration ash is 80%, the decomposition effect of waste incineration ash is relatively poor, but the cost is greatly reduced.

在一些实施例中，垃圾焚灰的粒径在50-250微米之间，煤粉的粒径在50-250微米之间，不可燃粉体掺混物的粒径在50-250微米之间。由此，使得垃圾焚灰和煤粉在燃烧处理器100内燃烧更充分，也使得不可燃粉体掺混物和重金属元素的接触效果更好。In some embodiments, the particle size of the refuse incineration ash is between 50-250 microns, the particle size of the pulverized coal is between 50-250 microns, and the particle size of the non-combustible powder blend is between 50-250 microns . As a result, the waste incineration ash and pulverized coal are more fully burned in the combustion processor 100, and the contact effect between the non-combustible powder admixture and the heavy metal element is also better.

在一些实施例中，如图3所示，供料组件5包括煤粉管51和回流帽52。煤粉管51沿第一腔102的轴线设在第一腔102内，煤粉管51具有入口端(例如图3中煤粉管51的左端)和出口端(例如图3中煤粉管51的右端)。调温导风筒3套设在煤粉管51的入口端处，回流帽52设在煤粉管51的出口端，回流帽52大体为筒形，回流帽52的出口朝向煤粉管51的入口端。In some embodiments, as shown in FIG. 3 , the feed assembly 5 includes a pulverized coal pipe 51 and a return cap 52 . The pulverized coal pipe 51 is arranged in the first cavity 102 along the axis of the first cavity 102, and the pulverized coal pipe 51 has an inlet end (for example, the left end of the pulverized coal pipe 51 in FIG. 3 ) and an outlet end (for example, the pulverized coal pipe 51 in FIG. 3 ) right end). The temperature regulation air guide tube 3 is sleeved at the inlet end of the pulverized coal pipe 51, and the return cap 52 is arranged at the outlet end of the pulverized coal pipe 51. entry port.

具体地，如图3所示，煤粉管51为直管形结构，垃圾焚灰、煤粉和不可燃粉体掺混物在气流的带动下从煤粉管51的左端进入煤粉管51。回流帽52设在煤粉管51的右端处，回流帽52的左端撇开、右端封闭，上述粉体从煤粉管51的右端冲出后会撞击在回流帽52的右端上，反射后的粉体从回流帽52的左端冲出并流向第一腔102的内部。Specifically, as shown in FIG. 3 , the pulverized coal pipe 51 has a straight tubular structure, and the mixture of garbage incineration ash, pulverized coal and non-combustible powder enters the pulverized coal pipe 51 from the left end of the pulverized coal pipe 51 under the driving of the airflow. . The return cap 52 is set at the right end of the pulverized coal pipe 51. The left end of the return cap 52 is left open and the right end is closed. The body is flushed out of the left end of the return cap 52 and flows into the interior of the first cavity 102 .

其中，上述粉体先撞击在回流帽52的右端上，再反射到第一腔102内，使得粉体的粒径更小、粉体更细化，有利于提高燃烧效率。Wherein, the above-mentioned powder hits the right end of the recirculation cap 52 first, and then is reflected into the first cavity 102, so that the particle size of the powder is smaller and the powder is more refined, which is beneficial to improve the combustion efficiency.

在一些实施例中，如图4所示，贴壁导风筒1包括筒体12和套设在筒体12的外周面上的柔性部13。In some embodiments, as shown in FIG. 4 , the wall-mounted air guide tube 1 includes a cylindrical body 12 and a flexible portion 13 sleeved on the outer peripheral surface of the cylindrical body 12 .

具体地，如图4所示，调节件71可以为螺栓，调节件71的第一部分为螺栓的螺纹部，调节件71的第二部分为螺帽部。柔性部13的内周面和筒体12的外周面相连，安装孔14为螺纹孔，调节件71的螺纹部设在安装孔14内，通过拧紧调节件71可使调节件71的螺帽部压紧柔性部13，使得柔性部13的外径缩小(体积缩小)，由此，扩大了柔性部13的外周面和周壁103之间的间隙，即扩大了贴壁风通道11的流通面积。Specifically, as shown in FIG. 4 , the adjusting member 71 may be a bolt, the first part of the adjusting member 71 is the threaded part of the bolt, and the second part of the adjusting member 71 is the nut part. The inner peripheral surface of the flexible portion 13 is connected with the outer peripheral surface of the cylinder body 12 , the mounting hole 14 is a threaded hole, and the threaded portion of the adjusting member 71 is set in the mounting hole 14 , and the nut portion of the adjusting member 71 can be adjusted by tightening the adjusting member 71 . The flexible portion 13 is compressed to reduce the outer diameter (volume reduction) of the flexible portion 13 , thereby expanding the gap between the outer peripheral surface of the flexible portion 13 and the peripheral wall 103 , that is, expanding the flow area of the adhering air passage 11 .

其中，密封垫圈72设在调节件71的螺帽部和柔性部13之间，密封垫圈72可用于密封安装孔14，使得贴壁风通道11与助燃风通道21之间不发生气体交换，有利于提高燃烧处理器100的密封性。同时，调节件71为刚性材料，密封垫圈72避免了调节件71直接压紧在柔性部13上，防止调节件71刮伤柔性部13，有利于延长柔性部13的使用寿命。The sealing washer 72 is provided between the nut part and the flexible part 13 of the adjusting member 71. The sealing washer 72 can be used to seal the mounting hole 14, so that no gas exchange occurs between the wall-mounted air passage 11 and the combustion-supporting air passage 21. It is beneficial to improve the sealing performance of the combustion processor 100 . Meanwhile, the adjusting member 71 is a rigid material, and the sealing gasket 72 prevents the adjusting member 71 from directly pressing on the flexible portion 13 , prevents the adjusting member 71 from scratching the flexible portion 13 , and is beneficial to prolong the service life of the flexible portion 13 .

在一些实施例中，如图3所示，燃烧处理器100进一步包括叶轮组件6，助燃风通道21、调温通道32和调温通道32内均设有叶轮组件6，叶轮组件6包括彼此相连的叶片61和伸缩杆62，伸缩杆62沿第一腔102的轴向设置。In some embodiments, as shown in FIG. 3 , the combustion processor 100 further includes an impeller assembly 6 , and the combustion air passage 21 , the temperature adjustment passage 32 and the temperature adjustment passage 32 are all provided with an impeller assembly 6 , and the impeller assemblies 6 are connected to each other. The blade 61 and the telescopic rod 62 are arranged along the axial direction of the first cavity 102 .

具体地，如图3所示，伸缩杆62可沿第一腔102的轴线设在上述气体通道内，伸缩杆62的左端可与构成上述通道的导风筒相连，伸缩杆62的右端设有叶片61，叶片61可自由旋转，上述通道内的气体在进入第一腔102内时会流经叶片61，叶片61使得流经叶片61的气体发生旋转并流向第一腔102的中心位置。由此，使得助燃气体、调温气体和废气之间的混合更充分，有利于提高废气的处理效果。Specifically, as shown in FIG. 3 , the telescopic rod 62 can be arranged in the above-mentioned gas channel along the axis of the first cavity 102 , the left end of the telescopic rod 62 can be connected with the air guide tube constituting the above-mentioned channel, and the right end of the telescopic rod 62 is provided with The vane 61, the vane 61 can rotate freely, the gas in the above-mentioned passage will flow through the vane 61 when entering the first cavity 102, and the vane 61 makes the gas flowing through the vane 61 rotate and flow to the center of the first cavity 102. Thereby, the mixing between the combustion-supporting gas, the temperature-adjusting gas and the exhaust gas is more sufficient, which is beneficial to improve the treatment effect of the exhaust gas.

在一些实施例中，如图5-图7所示，燃烧处理器100进一步包括煤粉分离器8，煤粉分离器8设在煤粉管51的入口端，煤粉分离器8为喉口形分离器81、齿轮形分离器82或花瓣形分离器83。In some embodiments, as shown in FIGS. 5-7 , the combustion processor 100 further includes a pulverized coal separator 8 , which is arranged at the inlet end of the pulverized coal pipe 51 , and the pulverized coal separator 8 is throat-shaped. Separator 81 , gear-shaped separator 82 or petal-shaped separator 83 .

在一些实施例中，如图2所示，调温导风筒3具有沿煤粉管51的轴向相对设置的第一端(例如图2中调温导风筒3的左端)和第二端(例如图2中调温导风筒3的右端)。调温导风筒3的第一端敞开，调温导风筒3的第二端上设有多个通孔(未示出)。燃烧处理器100进一步包括火焰检测器(未示出)和点火器(未示出)，火焰检测器和点火器设在调温导风筒3内，点火器的火焰穿过通孔后射入第一腔102内。In some embodiments, as shown in FIG. 2 , the temperature-adjusting air guide duct 3 has a first end (eg, the left end of the temperature-adjusting air guide duct 3 in FIG. 2 ) and a second oppositely disposed along the axial direction of the pulverized coal pipe 51 . end (for example, the right end of the temperature-adjusting air guide tube 3 in FIG. 2 ). The first end of the temperature regulation air guide tube 3 is open, and a plurality of through holes (not shown) are provided on the second end of the temperature regulation air guide tube 3 . The combustion processor 100 further includes a flame detector (not shown) and an igniter (not shown), the flame detector and the igniter are arranged in the temperature-adjusting air guide duct 3, and the flame of the igniter is injected into the through hole after passing through. inside the first cavity 102 .

具体地，如图2所示，调温导风筒3大体为桶形，调温导风筒3的右端为圆板形结构，调温导风筒3的右端朝向第一腔102的内部，火焰检测器和点火器设在煤粉管51的外周面和调温导风筒3的内周面之间，其中，点火器用于点燃第一腔102内的煤粉和废气，火焰检测器用于检测煤粉管51的外周面和调温导风筒3的内周面之间是否存在火焰，有利于提高燃烧处理器100的安全性。Specifically, as shown in FIG. 2 , the temperature adjustment air guide tube 3 is generally barrel-shaped, the right end of the temperature adjustment air guide tube 3 is a disc-shaped structure, and the right end of the temperature adjustment air guide tube 3 faces the inside of the first cavity 102 . The flame detector and the igniter are arranged between the outer peripheral surface of the pulverized coal pipe 51 and the inner peripheral surface of the temperature-adjusting air duct 3, wherein the igniter is used for igniting the pulverized coal and exhaust gas in the first chamber 102, and the flame detector is used for Detecting whether there is a flame between the outer peripheral surface of the pulverized coal pipe 51 and the inner peripheral surface of the temperature-adjusting air guide duct 3 is beneficial to improve the safety of the combustion processor 100 .

在一些实施例中，当燃烧处理器100的周壁103的温度高于预设温度时，压缩贴壁导风筒1的柔性部以扩大贴壁风通道11的流通面积，可选地，预设温度为40℃，当周壁103的温度高于40℃时，可扩大贴壁风通道11的流通面积，增大空气的流量，有利于更快的降低周壁103的温度。In some embodiments, when the temperature of the peripheral wall 103 of the combustion processor 100 is higher than a preset temperature, the flexible part of the wall-mounted air guide duct 1 is compressed to expand the flow area of the wall-mounted air passage 11 , optionally, a predetermined temperature When the temperature is 40°C, when the temperature of the peripheral wall 103 is higher than 40°C, the flow area of the wall-mounted air passage 11 can be enlarged, and the air flow rate can be increased, which is beneficial to reduce the temperature of the peripheral wall 103 more quickly.

在一些实施例中，燃烧处理器100的燃烧温度在900-1600℃，在该温度范围内可将垃圾焚灰充分分解。In some embodiments, the combustion temperature of the combustion processor 100 is 900-1600° C., within this temperature range, the refuse incineration ash can be fully decomposed.

实施例4：Example 4:

如图3-图8、图12和图14所示，根据本申请实施例的燃烧处理器100包括壳体101、贴壁导风筒1、助燃导风筒4、调温导风筒2和粉体供应组件。As shown in FIGS. 3-8 , 12 and 14 , a combustion processor 100 according to an embodiment of the present application includes a housing 101 , a wall-mounted air guide 1 , a combustion-supporting air guide 4 , a temperature-adjusting air guide 2 , and a Powder supply components.

壳体101具有第一腔102和围成第一腔102的周壁103。The housing 101 has a first cavity 102 and a peripheral wall 103 surrounding the first cavity 102 .

贴壁导风筒1设在第一腔102内，贴壁导风筒1的外周面和周壁103内周面之间形成贴壁风通道11，助燃导风筒4设在第一腔102内，助燃导风筒4的外周面与贴壁导风筒1的内周面之间形成助燃风通道41，粉体供应组件设在第一腔102内，调温导风筒2设在第一腔102内，调温导风筒2套设在粉体供应组件上，调温导风筒2的内周面与粉体供应组件的外周面之间形成过渡通道31，调温导风筒2的外周面与助燃导风筒4的内周面之间形成调温通道21。The wall-adhering air duct 1 is arranged in the first cavity 102 , a wall-adhering air channel 11 is formed between the outer peripheral surface of the wall-adhering air duct 1 and the inner peripheral surface of the peripheral wall 103 , and the combustion-supporting air duct 4 is arranged in the first cavity 102 , a combustion-supporting air channel 41 is formed between the outer peripheral surface of the combustion-supporting air guide duct 4 and the inner peripheral surface of the wall-mounted air guide duct 1, the powder supply component is set in the first cavity 102, and the temperature-adjusting air guide duct 2 is set in the first cavity 102. In the cavity 102, the temperature-adjusting air guide 2 is sleeved on the powder supply assembly, and a transition channel 31 is formed between the inner peripheral surface of the temperature-adjusting air guide 2 and the outer peripheral surface of the powder supply assembly, and the temperature-adjusting air guide 2 A temperature adjustment channel 21 is formed between the outer peripheral surface of the combustion-supporting air guide tube 4 and the inner peripheral surface of the combustion-supporting air guide tube 4 .

具体地，如图1-图5所示，壳体101的左端和右端大体为圆柱形，壳体101的中间段大体为圆锥形，壳体101的右端为整流腔1022，壳体101的中间段为稳燃腔1021，贴壁导风筒1、助燃导风筒4、调温导风筒2和粉体供应组件均设在壳体101左端内部。Specifically, as shown in FIGS. 1-5 , the left and right ends of the casing 101 are generally cylindrical, the middle section of the casing 101 is generally conical, the right end of the casing 101 is a rectifier cavity 1022 , and the middle of the casing 101 is The section is the combustion stabilization chamber 1021 , and the wall-mounted air guide 1, the combustion-supporting air guide 4, the temperature-adjusting air guide 2 and the powder supply assembly are all arranged inside the left end of the housing 101.

其中，供料组件5沿左右方向水平设置，且供料组件5的轴线和第一腔102的轴线大体重合，即供料组件5位于第一腔102的中间位置，由此，可使得生物质粉或生物质粉与煤粉的混合物通过供料组件5进入第一腔102后也处在第一腔102的中间位置，使得生物质粉或生物质粉与煤粉的混合物燃烧更充分。Wherein, the feeding assembly 5 is arranged horizontally along the left-right direction, and the axis of the feeding assembly 5 is substantially coincident with the axis of the first cavity 102, that is, the feeding assembly 5 is located in the middle of the first cavity 102, so that the biomass can be After entering the first cavity 102 through the feeding component 5, the powder or the mixture of biomass powder and coal powder is also in the middle position of the first chamber 102, so that the biomass powder or the mixture of biomass powder and coal powder is burned more fully.

贴壁导风筒1、助燃导风筒4、调温导风筒2均设在壳体101的左端的内侧，其中，调温导风筒2套设在供料组件5的左端上，助燃导风筒4套设在调温导风筒2上，贴壁导风筒1套设在助燃导风筒4上，且在第一腔102的轴向方向上，贴壁导风筒1的右端、助燃导风筒4的右端和调温导风筒2的右端大体对齐，本申请采用多通道配风的设计，空气经多级配风进入第一腔102内，气流边界处湍流强度强烈，加强了风粉混合速率，不仅使生物质粉或生物质粉与煤粉的掺混物粉稳定着火，还能保证其高效低氮燃烧，而且本申请的多通道配风的设计可以形成稳燃腔1021和整流腔1022壁面有贴壁冷却风的多层火焰结构，助燃风缓缓渗入主火焰，确保主火焰中间是高温、高CO和低氧的环境，延长生物质粉或生物质粉与煤粉的掺混物在高温、还原性气氛下的停留时间，达到高燃烧效率和低氮的目的，同时，贴壁风可以在稳燃腔1021内形成沿稳燃腔1021壁面流动的冷却空气层，以冷却稳燃腔1021和整流腔1022，使稳燃腔1021和整流腔1022的壁面温度始终低于40℃，不仅可以取消稳燃腔1021的水冷装置，而且避免稳燃腔1021壁面积灰结焦现象的发生。The wall-mounted air guide 1, the combustion-supporting air guide 4, and the temperature-adjusting air guide 2 are all arranged on the inner side of the left end of the housing 101, wherein the temperature-adjusting air guide 2 is sleeved on the left end of the feed assembly 5 to support combustion. The air guide duct 4 is sleeved on the temperature-adjusting air guide duct 2, and the wall-mounted air guide duct 1 is sleeved on the combustion-supporting air guide duct 4, and in the axial direction of the first cavity 102, the wall-mounted air guide duct 1 is sleeved. The right end, the right end of the combustion-supporting air guide duct 4 and the right end of the temperature-adjusting air guide duct 2 are generally aligned. The application adopts the design of multi-channel air distribution, and the air enters the first cavity 102 through the multi-stage air distribution, and the turbulent intensity at the airflow boundary is strong. , the mixing rate of air and powder is strengthened, which not only makes the biomass powder or the blend powder of biomass powder and coal powder ignite stably, but also ensures its high-efficiency and low-nitrogen combustion, and the multi-channel air distribution design of the present application can form a stable The walls of the combustion chamber 1021 and the rectification chamber 1022 have a multi-layer flame structure with wall-mounted cooling air, and the combustion-supporting air slowly penetrates into the main flame, ensuring that the middle of the main flame is a high temperature, high CO and low oxygen environment, and prolonging the biomass powder or biomass powder. The residence time of the mixture with pulverized coal in a high temperature and reducing atmosphere achieves the purpose of high combustion efficiency and low nitrogen. At the same time, the wall-adhering wind can form a cooling flow in the stable combustion chamber 1021 along the wall of the stable combustion chamber 1021 The air layer is used to cool the combustion stabilization chamber 1021 and the rectification chamber 1022, so that the wall temperature of the combustion stabilization chamber 1021 and the rectification chamber 1022 is always lower than 40°C, which can not only cancel the water cooling device of the combustion stabilization chamber 1021, but also avoid the wall The occurrence of area ash coking phenomenon.

由此，本申请实施例的燃烧处理器100具有高效燃烧，减少氮氧化物产生以及避免稳燃腔1021壁面积灰结焦等优点。Therefore, the combustion processor 100 of the embodiment of the present application has the advantages of efficient combustion, reduction of nitrogen oxide generation, and avoidance of ash coking in the wall area of the combustion stabilization chamber 1021 .

本申请实施例中的调温气体用于调节第一腔102内的燃烧温度，即当第一腔102内的燃烧温度高于预设值时，可向第一腔102内充入惰性气体，该惰性气体用于抑制第一腔102内的燃烧程度，以降低第一腔102内的燃烧温度，其中，惰性气体包括CO ₂、N ₂和其它惰性气体中的一种或多种； The temperature-adjusting gas in the embodiment of the present application is used to adjust the combustion temperature in the first cavity 102, that is, when the combustion temperature in the first cavity 102 is higher than a preset value, the first cavity 102 can be filled with an inert gas, The inert gas is used to suppress the degree of combustion in the first chamber 102 to reduce the combustion temperature in the first chamber 102, wherein the inert gas includes one or more of CO ₂ , N ₂ and other inert gases;

当第一腔102内的燃烧温度低于预设值时，可向第一腔102内充入氧化性气体和/或可燃气体，有利于提高第一腔102内的燃烧温度，其中，氧化性气体包括空气、氧气，可燃气体包括H ₂、CH ₄和天然气。 When the combustion temperature in the first cavity 102 is lower than the preset value, oxidizing gas and/or combustible gas may be charged into the first cavity 102, which is beneficial to increase the combustion temperature in the first cavity 102, wherein the oxidizing gas Gases include air, oxygen, and combustible gases include H ₂ , CH ₄ and natural gas.

优选地，本申请实施例的燃烧处理器100内的燃烧区温度控制在900-1600℃之间，在该温度范围内，可使生物质粉或生物质粉与煤粉的掺混物高效燃烧并减少氮氧化物的产生。Preferably, the temperature of the combustion zone in the combustion processor 100 of the embodiment of the present application is controlled between 900-1600° C. Within this temperature range, biomass powder or a blend of biomass powder and coal powder can be efficiently burned and reduce the production of nitrogen oxides.

在一些实施例中，如图2～图4所示，供料组件5包括风粉管55和回流帽52，风粉管55沿第一腔102的轴线设在第一腔102内，风粉管55具有入口端(例如图2～图4中风粉管55的左端)和出口端(例如图2～图4中风粉管55的右端)，调温导风筒2套设在风粉管55的入口端处，回流帽52设在风粉管55的出口端，回流帽52大体为筒形，还可以为圆锥形、椭圆形或圆柱形钝体，回流帽52的出口朝向风粉管55的入口端。In some embodiments, as shown in FIGS. 2 to 4 , the feeding assembly 5 includes an air powder pipe 55 and a return cap 52 . The air powder pipe 55 is arranged in the first cavity 102 along the axis of the first cavity 102 . The pipe 55 has an inlet end (for example, the left end of the air powder pipe 55 in FIGS. 2 to 4 ) and an outlet end (for example, the right end of the air powder pipe 55 in FIGS. 2 to 4 ). At the inlet end, the return cap 52 is arranged at the outlet end of the air powder pipe 55, the return cap 52 is generally cylindrical, and can also be a conical, elliptical or cylindrical blunt body, and the outlet of the return cap 52 faces the air powder pipe 55. entry port.

具体地，如图2～图4所示，风粉管55为直管形结构，生物质粉或生物质粉与煤粉的掺混物在气流的带动下从风粉管55的左端进入风粉管55，生物质粉或生物质粉与煤粉的掺混物在风粉管55内向右移动，回流帽52设在风粉管55的右端处，回流帽52的左端敞开、右端封闭，生物质粉或生物质粉与煤粉的掺混物从风粉管55的右端冲出后会撞击在回流帽52的右端上，反射后的生物质粉或生物质粉与煤粉的掺混物从回流帽52的左端冲出并流向第一腔102的内部。Specifically, as shown in FIGS. 2 to 4 , the air powder pipe 55 has a straight tubular structure, and the biomass powder or the mixture of biomass powder and coal powder enters the air powder from the left end of the air powder pipe 55 under the driving of the airflow. The powder pipe 55, the biomass powder or the mixture of biomass powder and coal powder moves to the right in the air powder pipe 55, the return cap 52 is arranged at the right end of the air powder pipe 55, the left end of the return cap 52 is open and the right end is closed, After the biomass powder or the mixture of biomass powder and coal powder is punched out from the right end of the air powder pipe 55, it will hit the right end of the return cap 52, and the reflected biomass powder or biomass powder and coal powder will be mixed. The material is flushed out from the left end of the return cap 52 and flows into the interior of the first cavity 102 .

其中，生物质粉或生物质粉与煤粉的掺混物先撞击在回流帽52的右端上，再反射到第一腔102内，使得生物质粉或生物质粉与煤粉的掺混物的粒径更小、生物质粉或生物质粉与煤粉的掺混物更细化，有利于提高生物质粉或生物质粉与煤粉的掺混物的燃烧效率。同时，经过反射后的生物质粉或生物质粉与煤粉的掺混物会弥散在第一腔102内，也使得生物质粉或生物质粉与煤粉的掺混物与空气或调温气体的接触更充分，有利于生物质粉或生物质粉与煤粉的掺混物的充分燃烧。Among them, the biomass powder or the mixture of biomass powder and coal powder first hits the right end of the return cap 52, and then is reflected into the first cavity 102, so that the biomass powder or the mixture of biomass powder and coal powder is The particle size is smaller, and the biomass powder or the blend of biomass powder and coal powder is more refined, which is beneficial to improve the combustion efficiency of biomass powder or the blend of biomass powder and coal powder. At the same time, the reflected biomass powder or the mixture of biomass powder and coal powder will be dispersed in the first cavity 102, which also makes the biomass powder or the mixture of biomass powder and coal powder mix with air or temperature adjustment. The contact of the gas is more complete, which is beneficial to the full combustion of the biomass powder or the blend of biomass powder and coal powder.

在一些实施例中，如图4所示，燃烧处理器100进一步包括叶轮组件6，助燃风通道41和调温通道21内均设有叶轮组件6，叶轮组件6包括彼此相连的叶片61和伸缩杆62，伸缩杆62沿第一腔102的轴向设置。In some embodiments, as shown in FIG. 4 , the combustion processor 100 further includes an impeller assembly 6 , the combustion air passage 41 and the temperature adjustment passage 21 are both provided with an impeller assembly 6 , and the impeller assembly 6 includes blades 61 connected to each other and a telescopic The rod 62 and the telescopic rod 62 are arranged along the axial direction of the first cavity 102 .

具体地，如图6所示，伸缩杆62可沿第一腔102的轴线设在上述气体通道内，伸缩杆62的左端可与构成上述通道的导风筒相连，伸缩杆62的右端设有叶片61，叶片61可自由旋转，上述通道内的气体在进入第一腔102内时会流经叶片61，叶片61使得流经叶片61的气体发生旋转并流向第一腔102的中心位置。由此，使得助燃气体和调温气体之间的混合更充分，有利于提高生物质粉或生物质粉与煤粉的掺混物的燃烧效率。Specifically, as shown in FIG. 6 , the telescopic rod 62 can be arranged in the above-mentioned gas channel along the axis of the first cavity 102 , the left end of the telescopic rod 62 can be connected with the air guide tube constituting the above-mentioned channel, and the right end of the telescopic rod 62 is provided with The vane 61, the vane 61 can rotate freely, the gas in the above-mentioned passage will flow through the vane 61 when entering the first cavity 102, and the vane 61 makes the gas flowing through the vane 61 rotate and flow to the center of the first cavity 102. Therefore, the mixing between the combustion-supporting gas and the temperature-adjusting gas is more sufficient, which is beneficial to improve the combustion efficiency of the biomass powder or the mixture of biomass powder and coal powder.

在一些实施例中，如图7所示，贴壁导风筒1包括筒体12和套设在筒体12的外周面上的柔性部13。In some embodiments, as shown in FIG. 7 , the wall-mounted air guide tube 1 includes a cylindrical body 12 and a flexible portion 13 sleeved on the outer peripheral surface of the cylindrical body 12 .

燃烧处理器100进一步包括调节组件，调节组件包括调节件71和密封垫圈72，筒体12上设有安装孔，调节件71的第一部分穿过柔性部13且设在安装孔内，调节件71的第二部分压制在柔性部13的外周面上，密封垫圈72设在调节件71的第二部分和柔性部13的外周面之间。The combustion processor 100 further includes an adjustment assembly, the adjustment assembly includes an adjustment member 71 and a sealing gasket 72, a mounting hole is provided on the cylinder 12, the first part of the adjustment member 71 passes through the flexible portion 13 and is arranged in the installation hole, the adjustment member 71 The second part of the 71 is pressed on the outer peripheral surface of the flexible part 13 , and the sealing gasket 72 is provided between the second part of the adjusting member 71 and the outer peripheral surface of the flexible part 13 .

具体地，如图7所示，调节件71可以为螺栓，调节件71的第一部分为螺栓的螺纹部，调节件71的第二部分为螺帽部。柔性部13的内周面和筒体12的外周面相连，安装孔为螺纹孔，调节件71的螺纹部设在安装孔内，通过拧紧调节件71可使调节件71的螺帽部压紧柔性部13，使得柔性部13的外径缩小(体积缩小)，由此，扩大了柔性部13的外周面和周壁103之间的间隙，即扩大了贴壁风通道11的流通面积。Specifically, as shown in FIG. 7 , the adjusting member 71 may be a bolt, the first part of the adjusting member 71 is a threaded portion of the bolt, and the second portion of the adjusting member 71 is a nut portion. The inner peripheral surface of the flexible portion 13 is connected to the outer peripheral surface of the cylinder body 12 , the mounting hole is a threaded hole, and the threaded portion of the adjusting member 71 is arranged in the mounting hole, and the nut portion of the adjusting member 71 can be compressed by tightening the adjusting member 71 The flexible portion 13 reduces the outer diameter (reduces the volume) of the flexible portion 13 , thereby expanding the gap between the outer peripheral surface of the flexible portion 13 and the peripheral wall 103 , that is, expanding the flow area of the adhering air passage 11 .

其中，密封垫圈72设在调节件71的螺帽部和柔性部13之间，密封垫圈72可用于密封安装孔，使得贴壁风通道11与助燃风通道41之间不发生气体交换，有利于提高燃烧处理器100的密封性。同时，调节件71为刚性材料，密封垫圈72避免了调节件71直接压紧在柔性部13上，防止调节件71刮伤柔性部13，有利于延长柔性部13的使用寿命。Wherein, the sealing washer 72 is provided between the nut part and the flexible part 13 of the adjusting member 71, and the sealing washer 72 can be used to seal the installation hole, so that no gas exchange occurs between the wall-mounted air passage 11 and the combustion-supporting air passage 41, which is beneficial to The tightness of the combustion processor 100 is improved. Meanwhile, the adjusting member 71 is a rigid material, and the sealing gasket 72 prevents the adjusting member 71 from being directly pressed on the flexible portion 13 , prevents the adjusting member 71 from scratching the flexible portion 13 , and is beneficial to prolong the service life of the flexible portion 13 .

在一些实施例中，安装孔为多个，多个安装孔沿筒体12的周向间隔设置，调节组件为多个，多个调节组件一一对应地设在多个安装孔内。由此，增大了调节件71与柔性部13的接触面积，使得柔性部13的受力更均匀，有利于延长柔性部13的使用寿命。In some embodiments, there are a plurality of installation holes, the plurality of installation holes are arranged at intervals along the circumference of the cylindrical body 12 , there are a plurality of adjustment components, and the plurality of adjustment components are provided in the plurality of installation holes in a one-to-one correspondence. Therefore, the contact area between the adjusting member 71 and the flexible portion 13 is increased, so that the force on the flexible portion 13 is more uniform, which is beneficial to prolong the service life of the flexible portion 13 .

在一些实施例中，如图2～图4所示，调温导风筒2具有沿风粉管55的轴向相对设置的第一端(例如图中调温导风筒2的左端)和第二端(例如图中调温导风筒2的右端)。调温导风筒2的第一端敞开，调温导风筒2的第二端上设有多个通孔(图中未示出)。燃烧处理器100进一步包括火焰检测器(图中未示出)和点火器(图中未示出)，火焰检测器和点火器设在调温导风筒2内，点火器的火焰穿过通孔后射入第一腔102内。In some embodiments, as shown in FIGS. 2 to 4 , the temperature-adjusting air guide duct 2 has a first end (for example, the left end of the temperature-adjusting air guide duct 2 in the figure) that is oppositely disposed along the axial direction of the air powder pipe 55 ; The second end (for example, the right end of the temperature-adjusting air guide tube 2 in the figure). The first end of the temperature-adjusting air guide duct 2 is open, and the second end of the temperature-adjusting air guide duct 2 is provided with a plurality of through holes (not shown in the figure). The combustion processor 100 further includes a flame detector (not shown in the figure) and an igniter (not shown in the figure), the flame detector and the igniter are arranged in the temperature regulating air guide duct 2, and the flame of the igniter passes through the passage. The hole is then injected into the first cavity 102 .

具体地，如图2～图4所示，调温导风筒2大体为桶形，调温导风筒2的右端为圆板形结构，调温导风筒2的右端朝向第一腔102的内部，火焰检测器和点火器设在风粉管55的外周面和调温导风筒2的内周面之间，其中，点火器用于点燃第一腔102内的生物质粉或生物质粉与煤粉的掺混物和空气以及调温气体，火焰检测器用于检测风粉管55的外周面和调温导风筒2的内周面之间是否存在火焰，有利于提高燃烧处理器100的安全性。Specifically, as shown in FIG. 2 to FIG. 4 , the temperature-adjusting air guide duct 2 is generally barrel-shaped, the right end of the temperature-adjusting air guide duct 2 is a disc-shaped structure, and the right end of the temperature-adjusting air guide duct 2 faces the first cavity 102 . Inside, the flame detector and the igniter are arranged between the outer peripheral surface of the air powder pipe 55 and the inner peripheral surface of the temperature-adjusting air guide duct 2 , wherein the igniter is used to ignite the biomass powder or biomass in the first cavity 102 The mixture of powder and coal powder, air and temperature-adjusting gas, the flame detector is used to detect whether there is a flame between the outer peripheral surface of the pulverized powder pipe 55 and the inner peripheral surface of the temperature-adjusting air duct 2, which is beneficial to improve the combustion processor. 100's of security.

本申请实施例的燃烧处理器100实施的废气处理方法包括以下步骤：The exhaust gas treatment method implemented by the combustion processor 100 of the embodiment of the present application includes the following steps:

生物质粉与煤粉掺混后(掺混比20～100％)由空气经过风粉管55和回流帽52组成的回流通道输送至稳燃腔1021内，空气一路由助燃风通道41进入第一腔102，经轴向叶轮后形成具有切向速度的旋转风进入稳燃腔1021，形成高温回流区，温度可达900～1600℃，生物质粉或生物质粉与煤粉的掺混物在低氧、炙热的高温回流区内热解，并与多股旋转风束在过渡通道31的共同作用下混合在一起后形成一个多层的主火焰，调温通道21可通入氧化性气体(包括但不限于空气、氧气)、可燃气体(包括但不限于H2、CH4和天然气)以及惰性气体(包括但不限于CO2、N2)，若燃烧区温度较低则通入氧化性气体或可燃气体，温度较高则通入惰性气体，以维持燃烧区温度在900～1600℃之间，空气另一路自贴壁风通道11进入第一腔102，形成沿稳燃腔1021壁面流动的冷却空气层，以冷却稳燃腔1021和整流腔1022，防止壁面结焦，并且与主火焰经整流腔1022形成风包火的高速喷射多层火焰进入炉膛，其中轴向叶轮产生旋转风束的旋流数应控制在0.6～2范围内，生物质粉和煤粉的粒径90％为50～250μm。After the biomass powder and coal powder are mixed (the mixing ratio is 20-100%), the air is transported to the stable combustion chamber 1021 through the return channel composed of the air powder pipe 55 and the return cap 52, and the air enters the first combustion air channel 41 through the combustion-supporting air channel 41. A cavity 102, after passing through the axial impeller, a rotating wind with a tangential speed enters the stable combustion cavity 1021, forming a high temperature recirculation zone, the temperature can reach 900-1600 ℃, biomass powder or a mixture of biomass powder and coal powder It is pyrolyzed in the low-oxygen, hot high-temperature recirculation zone, and mixed with multiple rotating wind beams under the joint action of the transition channel 31 to form a multi-layer main flame, and the temperature-adjusting channel 21 can pass oxidizing gas (including but not limited to air, oxygen), combustible gas (including but not limited to H2, CH4 and natural gas) and inert gas (including but not limited to CO2, N2), if the temperature of the combustion zone is low, oxidizing gas or combustible gas is introduced When the temperature is higher, inert gas is introduced to maintain the temperature of the combustion zone between 900 and 1600°C. The other air enters the first cavity 102 from the wall-mounted air channel 11 to form cooling air flowing along the wall of the combustion-stabilizing cavity 1021. layer to cool the combustion stabilization chamber 1021 and the rectifier chamber 1022, prevent coking on the wall, and form a high-speed jet of multi-layer flame with the main flame through the rectifier chamber 1022 to enter the furnace, where the axial impeller generates a swirling flow rate of the rotating wind beam. It should be controlled within the range of 0.6 to 2, and 90% of the particle size of biomass powder and coal powder is 50 to 250 μm.

在本申请的描述中，需要理解的是，术语“中心”、“纵向”、“横向”、“长度”、“宽度”、“厚度”、“上”、“下”、“前”、“后”、“左”、“右”、“竖直”、“水平”、“顶”、“底”“内”、“外”、“顺时针”、“逆时针”、“轴向”、“径向”、“周向”等指示的方位或位置关系为基于附图所示的方位或位置关系，仅是为了便于描述本申请和简化描述，而不是指示或暗示所指的装置或元件必须具有特定的方位、以特定的方位构造和操作，因此不能理解为对本申请的限制。In the description of this application, it should be understood that the terms "center", "longitudinal", "lateral", "length", "width", "thickness", "upper", "lower", "front", " Rear, Left, Right, Vertical, Horizontal, Top, Bottom, Inner, Outer, Clockwise, Counterclockwise, Axial, The orientations or positional relationships indicated by "radial direction", "circumferential direction", etc. are based on the orientations or positional relationships shown in the accompanying drawings, which are only for the convenience of describing the present application and simplifying the description, rather than indicating or implying the indicated devices or elements. It must have a specific orientation, be constructed and operate in a specific orientation, and therefore should not be construed as a limitation of the present application.

此外，术语“第一”、“第二”仅用于描述目的，而不能理解为指示或暗示相对重要性或者隐含指明所指示的技术特征的数量。由此，限定有“第一”、“第二”的特征可以明示或者隐含地包括至少一个该特征。在本申请的描述中，“多个”的含义是至少两个，例如两个，三个等，除非另有明确具体的限定。In addition, the terms "first" and "second" are only used for descriptive purposes, and should not be construed as indicating or implying relative importance or implying the number of indicated technical features. Thus, a feature delimited with "first", "second" may expressly or implicitly include at least one of that feature. In the description of the present application, "plurality" means at least two, such as two, three, etc., unless expressly and specifically defined otherwise.

在本申请中，除非另有明确的规定和限定，术语“安装”、“相连”、“连接”、“固定”等术语应做广义理解，例如，可以是固定连接，也可以是可拆卸连接，或成一体；可以是机械连接，也可以是电连接或彼此可通讯；可以是直接相连，也可以通过中间媒介间接相连，可以是两个元件内部的连通或两个元件的相互作用关系，除非另有明确的限定。对于本领域的普通技术人员而言，可以根据具体情况理解上述术语在本申请中的具体含义。In this application, unless otherwise expressly specified and limited, the terms "installed", "connected", "connected", "fixed" and other terms should be understood in a broad sense, for example, it may be a fixed connection or a detachable connection , or integrated; it can be a mechanical connection or an electrical connection or can communicate with each other; it can be directly connected or indirectly connected through an intermediate medium, it can be the internal connection of two components or the interaction relationship between the two components, unless otherwise expressly qualified. For those of ordinary skill in the art, the specific meanings of the above terms in this application can be understood according to specific situations.

在本申请中，除非另有明确的规定和限定，第一特征在第二特征“上”或“下”可以是第一和第二特征直接接触，或第一和第二特征通过中间媒介间接接触。而且，第一特征在第二特征“之上”、“上方”和“上面”可是第一特征在第二特征正上方或斜上方，或仅仅表示第一特征水平高度高于第二特征。第一特征在第二特征“之下”、“下方”和“下面”可以是第一特征在第二特征正下方或斜下方，或仅仅表示第一特征水平高度小于第二特征。In this application, unless otherwise expressly stated and defined, a first feature "on" or "under" a second feature may be in direct contact with the first and second features, or the first and second features indirectly through an intermediary touch. Also, the first feature being "above", "over" and "above" the second feature may mean that the first feature is directly above or obliquely above the second feature, or simply means that the first feature is level higher than the second feature. The first feature being "below", "below" and "below" the second feature may mean that the first feature is directly below or diagonally below the second feature, or simply means that the first feature is at a lower level than the second feature.

在本申请中，术语“一个实施例”、“一些实施例”、“示例”、“具体示例”、或“一些示例”等意指结合该实施例或示例描述的具体特征、结构、材料或者特点包含于本申请的至少一个实施例或示例中。在本说明书中，对上述术语的示意性表述不必须针对的是相同的实施例或示例。而且，描述的具体特征、结构、材料或者特点可以在任一个或多个实施例或示例中以合适的方式结合。此外，在不相互矛盾的情况下，本领域的技术人员可以将本说明书中描述的不同实施例或示例以及不同实施例或示例的特征进行结合和组合。In this application, the terms "one embodiment," "some embodiments," "example," "specific example," or "some examples," etc., mean the specific features, structures, materials, or characteristics described in connection with the embodiment or example. Features are included in at least one embodiment or example of the present application. In this specification, schematic representations of the above terms are not necessarily directed to the same embodiment or example. Furthermore, the particular features, structures, materials or characteristics described may be combined in any suitable manner in any one or more embodiments or examples. Furthermore, those skilled in the art may combine and combine the different embodiments or examples described in this specification, as well as the features of the different embodiments or examples, without conflicting each other.

尽管上面已经示出和描述了本申请的实施例，可以理解的是，上述实施例是示例性的，不能理解为对本申请的限制，本领域的普通技术人员在本申请的范围内可以对上述实施例进行变化、修改、替换和变型。Although the embodiments of the present application have been shown and described above, it should be understood that the above embodiments are exemplary and should not be construed as limitations to the present application. Embodiments are subject to variations, modifications, substitutions and variations.

Claims

一种废气/废液/固废燃烧处理器，其特征在于，包括：A waste gas/waste liquid/solid waste combustion processor, characterized in that it includes:

壳体，所述壳体具有第一腔和围成所述第一腔的周壁，所述第一腔包括依次连通的导风腔、稳燃腔和整流腔；a casing, the casing has a first cavity and a peripheral wall surrounding the first cavity, and the first cavity includes an air guide cavity, a combustion stabilization cavity and a rectification cavity that are communicated in sequence;

供料组件，所述供料组件设在所述第一腔内；a feeding assembly, the feeding assembly is arranged in the first cavity;

导风筒，所述导风筒为多个，多个所述导风筒均设在所述所述第一腔内；an air guide tube, there are multiple air guide tubes, and the multiple air guide tubes are all arranged in the first cavity;

所述壳体和与之相邻的所述导风筒之间、所述供料组件和与之相邻的所述导风筒之间、相邻的两个所述导风筒之间形成通道。Formed between the casing and the adjacent air guide tubes, between the feeding assembly and the adjacent air guide tubes, and between the two adjacent air guide tubes aisle.
根据权利要求1所述的燃烧处理器，其特征在于，所述导风筒包括：The combustion processor of claim 1, wherein the air guide comprises:

调温导风筒，套设在所述供料组件的进液端，靠近所述供料组件进液端一端敞开，远离所述供料组件进液端一端封闭，所述调温导风筒的内周面与所述供料组件的外周面之间形成过渡通道；A temperature-adjusting air guide tube is sleeved on the liquid inlet end of the feeding assembly, one end close to the liquid inlet end of the feeding assembly is open, and one end away from the liquid inlet end of the feeding assembly is closed. A transition channel is formed between the inner peripheral surface of the feed assembly and the outer peripheral surface of the feeding assembly;

贴壁导风筒，设在所述第一腔内，所述贴壁导风筒的外周面和所述周壁的内周面之间形成贴壁风通道；The wall-adhering air guide tube is arranged in the first cavity, and a wall-adhering air channel is formed between the outer peripheral surface of the wall-adhering air guide tube and the inner peripheral surface of the peripheral wall;

助燃导风筒，设在所述第一腔内，所述助燃导风筒的外周面与所述贴壁导风筒的内周面之间形成助燃风通道；The combustion-supporting air guide is arranged in the first cavity, and a combustion-supporting air channel is formed between the outer peripheral surface of the combustion-supporting air guide and the inner peripheral surface of the wall-mounted air guide;

煤粉输送导风筒，所述煤粉输送导风筒的外周面与所述助燃导风筒的内周面之间、所述煤粉输送导风筒的内周面与所述调温导风筒的外周面之间，两者其中之一为煤粉输送通道，另一为调温通道。The pulverized coal conveying air duct, between the outer peripheral surface of the pulverized coal conveying air duct and the inner peripheral surface of the combustion-supporting air duct, the inner peripheral surface of the pulverized coal conveying air duct and the temperature adjustment guide Between the outer peripheral surfaces of the air duct, one of the two is a coal powder conveying channel, and the other is a temperature adjusting channel.
根据权利要求2所述的燃烧处理器，其特征在于，所述供料组件包括有机废液输送管、回流帽和雾化喷嘴组件，所述有机废液输送管与所述第一腔同轴设置，所述回流帽设在所述有机废液输送管的出液端，所述回流帽为筒形，所述回流帽的出口朝向所述有机废液输送管的进液端，所述雾化喷嘴组件设置在所述回流帽的出口处。The combustion processor according to claim 2, wherein the feeding component comprises an organic waste liquid conveying pipe, a return cap and an atomizing nozzle assembly, and the organic waste liquid conveying pipe is coaxial with the first cavity The return cap is arranged at the liquid outlet end of the organic waste liquid conveying pipe, the return cap is cylindrical, and the outlet of the return cap faces the liquid inlet end of the organic waste liquid conveying pipe, and the mist A chemical nozzle assembly is provided at the outlet of the return cap.
根据权利要求3所述的燃烧处理器，其特征在于，所述雾化喷嘴组件包括固定盘，所述固定盘套设在所述有机废液输送管的出液端外侧，所述固定盘的外周面与所述回流帽的出口端内边缘连接，所述固定盘上设置有多个贯穿所述固定盘的喷射孔。The combustion processor according to claim 3, wherein the atomizing nozzle assembly comprises a fixed disk, the fixed disk is sleeved on the outside of the liquid outlet end of the organic waste liquid conveying pipe, and the fixed disk is The outer peripheral surface is connected with the inner edge of the outlet end of the return cap, and the fixed disk is provided with a plurality of injection holes penetrating the fixed disk.
根据权利要求2-4中任一项所述的燃烧处理器，其特征在于，所述助燃风通道和所述调温通道内均设有轴向叶轮组件。The combustion processor according to any one of claims 2-4, wherein an axial impeller assembly is provided in the combustion air passage and the temperature adjustment passage.
根据权利要求2-5中任一项所述的燃烧处理器，其特征在于，所述贴壁导风筒包括筒体、套设在所述筒体的外周面上的柔性部和调节组件，所述调节组件包括调节件和密封垫圈，所述筒体上沿所述筒体的周向间隔设置有多个安装孔，每个所述安装孔对应设置一个所述调节件，所述调节组件的第一部分穿过所述柔性部且设在所述安装孔内，所述调节件的第二部分压制在所述柔性部的外周面上，所述密封垫圈设在所述调节件的所述第二部分和所述柔性部的外周面之间。The combustion processor according to any one of claims 2 to 5, wherein the wall-mounted air guide tube comprises a tube body, a flexible part and an adjustment component sleeved on the outer peripheral surface of the tube body, The adjustment assembly includes an adjustment piece and a sealing washer, a plurality of installation holes are arranged on the cylinder body at intervals along the circumferential direction of the cylinder body, and each of the installation holes is correspondingly provided with one of the adjustment pieces, and the adjustment assembly The first part of the flexible part passes through the flexible part and is provided in the mounting hole, the second part of the adjusting part is pressed on the outer peripheral surface of the flexible part, and the sealing gasket is provided on the said adjusting part. between the second portion and the outer peripheral surface of the flexible portion.
根据权利要求2-6中任一项所述的燃烧处理器，其特征在于，所述调温通道内部设置有点火器和火焰检测器。The combustion processor according to any one of claims 2-6, wherein an igniter and a flame detector are arranged inside the temperature regulation channel.
根据权利要求2-7中任一项所述的燃烧处理器，其特征在于，所述煤粉输送通道内侧沿其周向设置有多个浓淡分离结构件。The combustion processor according to any one of claims 2 to 7, characterized in that, a plurality of concentration-lean separation structural members are arranged on the inner side of the pulverized coal conveying channel along the circumferential direction thereof.
一种根据权利要求2-8中任一项所述的燃烧处理器的使用方法，其特征在于，包括以下步骤：A method of using a combustion processor according to any one of claims 2-8, characterized in that, comprising the steps of:

S1、根据有机废液的热值及废液量及煤种选择合适直径的所述有机废液输送管、合适雾化特性的所述雾化喷嘴组件及所述浓淡分离组件；S1, according to the calorific value of the organic waste liquid, the amount of waste liquid and the coal type, select the organic waste liquid conveying pipe of suitable diameter, the atomization nozzle assembly with suitable atomization characteristics, and the concentration separation assembly;

S2、分两路通入空气，一路空气经助燃风通道和调温通道进入所述第一腔，另一路经贴壁风通道进入所述第一腔；S2, the air is introduced into two paths, one air enters the first cavity through the combustion-supporting air channel and the temperature adjustment channel, and the other air enters the first cavity through the wall-mounted air channel;

S3、与步骤S2同时进行，煤粉气流点火后经煤粉输送通道进入第一腔；S3, performed simultaneously with step S2, the pulverized coal gas flow enters the first cavity through the pulverized coal conveying channel after ignition;

S4、通入有机废液，有机废液经有机废液输送管进入回流帽，然后经回流帽上的雾化喷嘴组件喷入第一腔。S4. The organic waste liquid is introduced, and the organic waste liquid enters the return cap through the organic waste liquid conveying pipe, and is then sprayed into the first cavity through the atomizing nozzle assembly on the return cap.
根据权利要求9所述的燃烧处理器的使用方法，其特征在于，步骤S2中可同时向调温通道内通入氧化性气体或惰性气体，以维持所述第一腔内的温度在700～1600℃之间。The method for using a combustion processor according to claim 9, wherein in step S2, an oxidizing gas or an inert gas can be introduced into the temperature-adjusting channel at the same time, so as to maintain the temperature in the first chamber between 700 and 700°C. between 1600°C.
根据权利要求9或10所述的燃烧处理器的使用方法，其特征在于，有机废液的入口压力大于所述第一腔内部的压力，控制在0.3～0.5MPa。The method for using a combustion processor according to claim 9 or 10, wherein the inlet pressure of the organic waste liquid is greater than the pressure inside the first chamber, and is controlled at 0.3-0.5MPa.
根据权利要求1所述的燃烧处理器，其特征在于，所述导风筒包括：The combustion processor of claim 1, wherein the air guide comprises:

贴壁导风筒，所述贴壁导风筒设在所述第一腔内，所述贴壁导风筒的外周面和所述周壁之间形成贴壁风通道；a wall-adhering air guide tube, the wall-adhering air guide tube is arranged in the first cavity, and a wall-adhering air channel is formed between the outer peripheral surface of the wall-adhering air guide tube and the peripheral wall;

调温导风筒，所述调温导风筒设在所述第一腔内，所述调温导风筒的外周面与所述贴壁导风筒的内周面之间形成调温通道；A temperature-adjusting air duct, the temperature-adjusting air duct is arranged in the first cavity, and a temperature-adjusting channel is formed between the outer peripheral surface of the temperature-adjusting air duct and the inner peripheral surface of the wall-mounted air duct ;

废气输送导风筒，所述废气输送导风筒设在所述第一腔内，所述废气输送导风筒套设在所述供料组件上，所述废气输送导风筒的内周面与所述供料组件的外周面之间形成过渡通道，所述废气输送导风筒的外周面与所述调温导风筒的内周面之间形成废气通道The exhaust gas conveying air guide tube, the exhaust gas conveying air guide tube is arranged in the first cavity, the exhaust gas conveying air guide tube is sleeved on the feeding component, and the inner peripheral surface of the exhaust gas conveying air guide tube is A transition channel is formed between the outer peripheral surface of the feeding assembly, and an exhaust gas channel is formed between the outer peripheral surface of the exhaust gas conveying air guide tube and the inner peripheral surface of the temperature adjustment air guide tube

助燃导风筒，所述助燃导风筒设在所述第一腔内，所述助燃导风筒在内外方向上位于所述贴壁导风筒和所述调温导风筒之间，所述助燃导风筒的外周面和所述贴壁导风筒的内周面之间形成助燃风通道，所述助燃导风筒的内周面和所述调温导风筒的外周面之间形成调温通道。Combustion-supporting air duct, the combustion-supporting air duct is arranged in the first cavity, and the combustion-supporting air duct is located between the wall-mounted air duct and the temperature-adjusting air duct in the inner and outer directions, so A combustion-supporting air channel is formed between the outer peripheral surface of the combustion-supporting air guide tube and the inner peripheral surface of the wall-mounted air guide tube, and a combustion-supporting air channel is formed between the inner peripheral surface of the combustion-supporting air guide tube and the outer peripheral surface of the temperature-adjusting air guide tube. Form a temperature control channel.
根据权利要求12所述的燃烧处理器，其特征在于，所述供料组件包括煤粉管和回流帽，所述煤粉管沿所述第一腔的轴线设在所述第一腔内，所述煤粉管具有入口端和出口端，所述废气输送导风筒套设在所述煤粉管的入口端处，所述回流帽设在所述煤粉管的出口端，所述回流帽大体为筒形，所述回流帽的出口朝向所述煤粉管的入口端。The combustion processor according to claim 12, wherein the feeding component comprises a pulverized coal pipe and a return cap, and the pulverized coal pipe is arranged in the first cavity along the axis of the first cavity, The pulverized coal pipe has an inlet end and an outlet end, the exhaust gas conveying air guide tube is sleeved at the inlet end of the pulverized coal pipe, the return cap is arranged at the outlet end of the pulverized coal pipe, and the return flow The cap is generally cylindrical, and the outlet of the return cap faces toward the inlet end of the pulverized coal pipe.
根据权利要求12或13所述的燃烧处理器，其特征在于，进一步包括叶轮组件，所述助燃风通道、所述调温通道和所述废气通道内均设有所述叶轮组件，所述叶轮组件包括彼此相连的叶片和伸缩杆，所述伸缩杆沿所述第一腔的轴向设置。The combustion processor according to claim 12 or 13, further comprising an impeller assembly, the impeller assembly is arranged in the combustion air passage, the temperature adjustment passage and the exhaust gas passage, and the impeller The assembly includes blades and telescopic rods connected to each other, the telescopic rods being arranged in the axial direction of the first cavity.
根据权利要求12-14中任一项所述的燃烧处理器，其特征在于，所述贴壁导风筒包括筒体和套设在所述筒体的外周面上的柔性部，所述燃烧处理器进一步包括调节组件，所述调节组件包括调节件和密封垫圈，所述筒体上设有安装孔，所述调节件的第一部分穿过所述柔性部且设在所述安装孔内，所述调节件的第二部分压制在所述柔性部的外周面上，所述密封垫圈设在所述调节件的所述第二部分和所述柔性部的外周面之间。The combustion processor according to any one of claims 12 to 14, wherein the wall-adhering air guide tube comprises a tube body and a flexible part sleeved on the outer peripheral surface of the tube body, and the combustion The processor further includes an adjustment assembly, the adjustment assembly includes an adjustment piece and a sealing gasket, a mounting hole is provided on the cylinder body, and a first part of the adjustment piece passes through the flexible portion and is arranged in the mounting hole, The second portion of the adjusting member is pressed on the outer peripheral surface of the flexible portion, and the sealing gasket is provided between the second portion of the adjusting member and the outer peripheral surface of the flexible portion.
根据权利要求12-15中任一项所述的燃烧处理器，其特征在于，进一步包括煤粉分离器，所述煤粉分离器设在所述煤粉管的入口端，所述煤粉分离器为喉口形分离器、齿轮形分离器或花瓣形分离器。The combustion processor according to any one of claims 12 to 15, further comprising a pulverized coal separator, the pulverized coal separator is arranged at the inlet end of the pulverized coal pipe, and the pulverized coal is separated The separator is a throat-shaped separator, a gear-shaped separator or a petal-shaped separator.
根据权利要求13或16所述的燃烧处理器，其特征在于，所述废气输送导风筒具有沿所述煤粉管的轴向相对设置的第一端和第二端，所述废气输送导风筒的第一端敞开，所述废气输送导风筒的第二端上设有多个通孔，所述燃烧处理器进一步包括火焰检测器和点火器，所述火焰检测器和所述点火器设在所述废气输送导风筒内，所述点火器的火焰穿过所述通孔后射入所述第一腔内。The combustion processor according to claim 13 or 16, wherein the exhaust gas conveying air guide duct has a first end and a second end oppositely arranged along the axial direction of the pulverized coal pipe, and the exhaust gas conveying guide The first end of the air duct is open, the second end of the exhaust gas conveying air guide duct is provided with a plurality of through holes, the combustion processor further comprises a flame detector and an igniter, the flame detector and the ignition The igniter is arranged in the exhaust gas conveying air guide tube, and the flame of the igniter is injected into the first cavity after passing through the through hole.
一种根据权利要求12-17中任一项所述的燃烧处理器的使用方法，其特征在于，包括以下步骤：A method of using a combustion processor according to any one of claims 12-17, characterized in that, comprising the steps of:

根据废气的热值、气量和所选用的煤种确定燃烧处理器内的燃烧温度；Determine the combustion temperature in the combustion processor according to the calorific value of the exhaust gas, the gas volume and the selected coal type;

废气通过废气通道进入所述燃烧处理器内；Exhaust gas enters into the combustion processor through the exhaust gas passage;

煤粉经过煤粉供料组件进入所述燃烧处理器内；The pulverized coal enters the combustion processor through the pulverized coal feeding component;

空气分成两路进入所述燃烧处理器内，其中，一路空气通过助燃风通道进入所述燃烧处理器内，另一炉空气通过贴壁风通道进入所述燃烧处理器内并形成贴壁风，贴壁风的至少一部分沿所述燃烧处理器的周壁流动形成冷却层；和The air enters the combustion processor in two ways, wherein one air enters the combustion processor through the combustion-supporting air channel, and the other furnace air enters the combustion processor through the wall-adhering air channel and forms the wall-adhering wind, at least a portion of the wall-to-wall wind flows along the peripheral wall of the combustion processor to form a cooling layer; and

点燃所述燃烧处理器内的煤粉和废气。The pulverized coal and exhaust gases within the combustion processor are ignited.
根据权利要求18所述的燃烧处理器的使用方法，其特征在于，当所述燃烧处理器的所述周壁的温度高于预设温度时，压缩所述贴壁导风筒的所述柔性部以扩大所述贴壁风通道的流通面积，可选地，所述预设温度为40℃。The method for using a combustion processor according to claim 18, wherein when the temperature of the peripheral wall of the combustion processor is higher than a preset temperature, the flexible portion of the wall-mounted air guide tube is compressed In order to expand the flow area of the wall-mounted air channel, optionally, the preset temperature is 40°C.
根据权利要求18或19所述的燃烧处理器的使用方法，其特征在于，包括：根据所述煤粉的煤种选用对应的煤粉分离器，所述煤粉分离器为喉口形分离器、齿轮形分离器或花瓣形分离器，可选地，所述废气为含有氟化物的废气。The method for using a combustion processor according to claim 18 or 19, characterized in that it comprises: selecting a corresponding pulverized coal separator according to the coal type of the pulverized coal, wherein the pulverized coal separator is a throat-shaped separator, A gear-shaped separator or a petal-shaped separator, optionally, the exhaust gas is an exhaust gas containing fluoride.
根据权利要求1所述的燃烧处理器，其特征在于，所述导风筒包括：The combustion processor of claim 1, wherein the air guide comprises:

贴壁导风筒，所述贴壁导风筒设在所述第一腔内，所述贴壁导风筒的外周面和所述周壁之间形成贴壁风通道；a wall-adhering air guide tube, the wall-adhering air guide tube is arranged in the first cavity, and a wall-adhering air channel is formed between the outer peripheral surface of the wall-adhering air guide tube and the peripheral wall;

助燃导风筒，所述助燃导风筒设在所述第一腔内，所述助燃导风筒的外周面与所述贴壁导风筒的内周面之间形成助燃风通道；a combustion-supporting air guide tube, the combustion-supporting air guide tube is arranged in the first cavity, and a combustion-supporting air channel is formed between the outer peripheral surface of the combustion-supporting air guide tube and the inner peripheral surface of the wall-mounted air guide tube;

调温导风筒，所述调温导风筒设在所述第一腔内，所述调温导风筒套设在所述供料组件上，所述调温导风筒的内周面与所述供料组件的外周面之间形成过渡通道，所述调温导风筒的外周面与所述助燃导风筒的内周面之间形成调温通道。The temperature regulation air guide tube is arranged in the first cavity, the temperature regulation air guide tube is sleeved on the feeding component, and the inner peripheral surface of the temperature regulation air guide tube is A transition channel is formed between the outer peripheral surface of the feed assembly and the outer peripheral surface of the temperature regulation air guide tube and the temperature regulation channel is formed between the outer peripheral surface of the temperature regulation air guide tube and the inner peripheral surface of the combustion-supporting air guide tube.
根据权利要求21所述的燃烧处理器，其特征在于，所述供料组件包括煤粉管和回流帽，所述煤粉管沿所述第一腔的轴线设在所述第一腔内，所述煤粉管具有入口端和出口端，所述调温导风筒套设在所述煤粉管的入口端处，所述回流帽设在所述煤粉管的出口端，所述回流帽大体为筒形，所述回流帽的出口朝向所述煤粉管的入口端。The combustion processor according to claim 21, wherein the feeding assembly comprises a pulverized coal pipe and a return cap, and the pulverized coal pipe is arranged in the first cavity along the axis of the first cavity, The pulverized coal pipe has an inlet end and an outlet end, the temperature regulation air guide tube is sleeved at the inlet end of the pulverized coal pipe, the return cap is arranged at the outlet end of the pulverized coal pipe, the return flow The cap is generally cylindrical, and the outlet of the return cap faces toward the inlet end of the pulverized coal pipe.
根据权利要求21或22所述的燃烧处理器，其特征在于，进一步包括叶轮组件，所述助燃风通道和所述调温通道内均设有所述叶轮组件，所述叶轮组件包括彼此相连的叶片和伸缩杆，所述伸缩杆沿所述第一腔的轴向设置。The combustion processor according to claim 21 or 22, further comprising an impeller assembly, the impeller assembly is arranged in the combustion-supporting air passage and the temperature adjustment passage, and the impeller assembly includes an impeller connected to each other. The blade and the telescopic rod are arranged along the axial direction of the first cavity.
根据权利要求21-23中任一项所述的燃烧处理器，其特征在于，所述贴壁导风筒包括筒体和套设在所述筒体的外周面上的柔性部，所述燃烧处理器进一步包括调节组件，所述调节组件包括调节件和密封垫圈，所述筒体上设有安装孔，所述调节件的第一部分穿过所述柔性部且设在所述安装孔内，所述调节件的第二部分压制在所述柔性部的外周面上，所述密封垫圈设在所述调节件的所述第二部分和所述柔性部的外周面之间。The combustion processor according to any one of claims 21-23, wherein the wall-adhering air guide tube comprises a tube body and a flexible part sleeved on the outer peripheral surface of the tube body, and the combustion The processor further includes an adjustment assembly, the adjustment assembly includes an adjustment piece and a sealing gasket, a mounting hole is provided on the cylinder body, and a first part of the adjustment piece passes through the flexible portion and is arranged in the mounting hole, The second portion of the adjusting member is pressed on the outer peripheral surface of the flexible portion, and the sealing gasket is provided between the second portion of the adjusting member and the outer peripheral surface of the flexible portion.
根据权利要求22所述的燃烧处理器，其特征在于，所述调温导风筒具有沿所述煤粉管的轴向相对设置的第一端和第二端，所述调温导风筒的第一端敞开，所述调温导风筒的第二端上设有多个通孔，所述燃烧处理器进一步包括火焰检测器和点火器，所述火焰检测器和所述点火器设在所述调温导风筒内，所述点火器的火焰穿过所述通孔后射入所述第一腔内。The combustion processor according to claim 22, wherein the temperature-adjusting air duct has a first end and a second end oppositely disposed along the axial direction of the pulverized coal pipe, and the temperature-adjusting air duct The first end of the air guide tube is open, the second end of the temperature-adjusting air guide tube is provided with a plurality of through holes, the combustion processor further includes a flame detector and an igniter, and the flame detector and the igniter are provided with In the temperature regulation air guide tube, the flame of the igniter is injected into the first cavity after passing through the through hole.
一种根据权利要求21-25中任一项所述的燃烧处理器的使用方法，其特征在于，包括以下步骤：A method of using a combustion processor according to any one of claims 21-25, characterized in that it comprises the following steps:

根据垃圾焚灰的成分确定所述燃烧处理器的燃烧温度；Determine the combustion temperature of the combustion processor according to the composition of the waste incineration ash;

所述垃圾焚灰和煤粉通过所述煤粉供料组件进入所述燃烧处理器内；The waste incineration ash and pulverized coal enter into the combustion processor through the pulverized coal feeding component;

空气分成两路进入所述燃烧处理器内，其中，一路空气通过助燃风通道进入所述燃烧处理器内，另一炉空气通过贴壁风通道进入所述燃烧处理器内并形成贴壁风，贴壁风的至少一部分沿所述燃烧处理器的周壁流动形成冷却层；和The air enters the combustion processor in two ways, wherein one air enters the combustion processor through the combustion-supporting air channel, and the other furnace air enters the combustion processor through the wall-adhering air channel and forms the wall-adhering wind, at least a portion of the wall-to-wall wind flows along the peripheral wall of the combustion processor to form a cooling layer; and

点燃所述燃烧处理器内的煤粉和所述垃圾焚灰。The pulverized coal and the refuse incineration ash in the combustion processor are ignited.
根据权利要求26所述的燃烧处理器的使用方法，其特征在于，进一步包括：在使所述垃圾焚灰和所述煤粉进入所述燃烧处理器内之前，将不可燃粉体掺混物、所述煤粉和所述垃圾焚灰混合以便利用所述不可燃粉体掺混物吸附所述垃圾焚灰熔融后的重金属元素，可选地，所述垃圾焚灰的质量占所述垃圾焚灰、所述煤粉与所述不可燃粉体掺混物的总质量的20％-80，所述垃圾焚灰的粒径在50-250微米之间，所述煤粉的粒径在50-250微米之间，所述不可燃粉体掺混物的粒径在50-250微米之间。The method for using a combustion processor according to claim 26, further comprising: before the waste incineration ash and the pulverized coal enter the combustion processor, mixing non-combustible powder , the coal powder and the refuse incineration ash are mixed so as to utilize the non-combustible powder admixture to absorb the heavy metal elements after the refuse incineration ash is melted. Optionally, the mass of the refuse incineration ash accounts for the 20%-80% of the total mass of the mixture of incineration ash, the coal powder and the non-combustible powder, the particle size of the garbage incineration ash is between 50-250 microns, and the particle size of the coal powder is between 50 and 250 microns. Between 50-250 microns, the particle size of the non-combustible powder blend is between 50-250 microns.
根据权利要求26或27所述的燃烧处理器的使用方法，其特征在于，所述垃圾焚灰的质量占所述垃圾焚灰与煤粉的总质量的20％-80％。The method for using a combustion processor according to claim 26 or 27, wherein the mass of the waste incineration ash accounts for 20%-80% of the total mass of the waste incineration ash and coal powder.
根据权利要求26-28中任一项所述的燃烧处理器的使用方法，其特征在于，当所述燃烧处理器的周壁的温度高于预设温度时，压缩所述贴壁导风筒的所述柔性部以扩大所述贴壁风通道的流通面积，可选地，所述预设温度为40℃。The method of using a combustion processor according to any one of claims 26-28, wherein when the temperature of the peripheral wall of the combustion processor is higher than a preset temperature, the compressed air of the wall-mounted air duct The flexible part is used to expand the flow area of the wall-adhering air channel. Optionally, the preset temperature is 40°C.
根据权利要求26-29中任一项所述的燃烧处理器的使用方法，其特征在于，所述燃烧处理器的燃烧温度在900-1600℃。The method for using a combustion processor according to any one of claims 26-29, wherein the combustion temperature of the combustion processor is 900-1600°C.
根据权利要求1所述的燃烧处理器，其特征在于，所述导风筒包括：The combustion processor of claim 1, wherein the air guide comprises:

贴壁导风筒，设在所述第一腔内，所述贴壁导风筒的外周面和所述周壁之间形成贴壁风通道；The wall-adhering air guide tube is arranged in the first cavity, and a wall-adhering air channel is formed between the outer peripheral surface of the wall-adhering air guide tube and the peripheral wall;

助燃导风筒，设在所述第一腔内，所述助燃导风筒的外周面与所述贴壁导风筒的内周面之间形成助燃风通道；The combustion-supporting air guide is arranged in the first cavity, and a combustion-supporting air channel is formed between the outer peripheral surface of the combustion-supporting air guide and the inner peripheral surface of the wall-mounted air guide;

过渡导风筒，设在所述第一腔内，所述过渡导风筒套设在所述供料组件上，所述过渡导风筒的内周面与所述供料组件的外周面之间形成过渡通道，所述过渡导风筒的外周面与所述助燃导风筒的内周面之间形成调温通道。The transition air guide tube is arranged in the first cavity, the transition air guide tube is sleeved on the feed assembly, and the inner peripheral surface of the transition air guide tube and the outer peripheral surface of the feed assembly are connected. A transition channel is formed between, and a temperature adjustment channel is formed between the outer peripheral surface of the transition air guide tube and the inner peripheral surface of the combustion-supporting air guide tube.
根据权利要求31所述的燃烧处理器，其特征在于，所述供料组件包括风粉管和回流帽，所述风粉管沿所述第一腔的轴线设在所述第一腔内，所述风粉管具有入口端和出口端，所述过渡导风筒套设在所述风粉管的入口端处，所述回流帽设在所述风粉管的出口端，所述回流帽为筒形，所述回流帽的出口朝向所述风粉管的入口端。The combustion processor according to claim 31, wherein the feeding component comprises an air powder pipe and a return cap, and the air powder pipe is arranged in the first cavity along the axis of the first cavity, The air-powder pipe has an inlet end and an outlet end, the transition air guide tube is sleeved at the inlet end of the air-powder pipe, and the return cap is arranged at the outlet end of the air-powder pipe. It is cylindrical, and the outlet of the return cap faces the inlet end of the air powder pipe.
根据权利要求31或32所述的燃烧处理器，其特征在于，所述助燃风通道和所述调温通道内均设有叶轮组件，所述叶轮组件包括彼此相连的叶片和伸缩杆，所述伸缩杆沿所述第一腔的轴向设置。The combustion processor according to claim 31 or 32, wherein an impeller assembly is arranged in the combustion air passage and the temperature adjustment passage, and the impeller assembly comprises blades and telescopic rods connected to each other, and the The telescopic rod is arranged along the axial direction of the first cavity.
根据权利要求31-33中任一项所述的燃烧处理器，其特征在于，所述贴壁导风筒包括筒体和套设在所述筒体的外周面上的柔性部，所述燃烧处理器进一步包括调节组件，所述调节组件包括调节件和密封垫圈，所述筒体上设有安装孔，所述调节件的第一部分穿过所述柔性部且设在所述安装孔内，所述调节件的第二部分压制在所述柔性部的外周面上，所述密封垫圈设在所述调节件的所述第二部分和所述柔性部的外周面之间。The combustion processor according to any one of claims 31-33, wherein the wall-mounted air guide tube comprises a tube body and a flexible part sleeved on the outer peripheral surface of the tube body, and the combustion The processor further includes an adjustment assembly, the adjustment assembly includes an adjustment piece and a sealing gasket, a mounting hole is provided on the cylinder body, and a first part of the adjustment piece passes through the flexible portion and is arranged in the mounting hole, The second portion of the adjusting member is pressed on the outer peripheral surface of the flexible portion, and the sealing gasket is provided between the second portion of the adjusting member and the outer peripheral surface of the flexible portion.
根据权利要求32所述的燃烧处理器，其特征在于，所述过渡导风筒具有沿所述风粉管的轴向相对设置的第一端和第二端，所述过渡导风筒的第一端敞开，所述过渡导风筒的第二端上设有多个通孔，所述燃烧处理器进一步包括点火器，所述点火器设在所述过渡导风筒内，所述点火器的火焰穿过所述通孔后射入所述第一腔内。The combustion processor according to claim 32, wherein the transition air duct has a first end and a second end oppositely disposed along the axial direction of the air powder duct, and the transition air duct has a first end and a second end. One end is open, the second end of the transition air guide tube is provided with a plurality of through holes, the combustion processor further includes an igniter, the igniter is arranged in the transition air guide tube, the igniter The flame passed through the through hole and then injected into the first cavity.
根据权利要求31-35中任一项所述的燃烧处理器，其特征在于，进一步包括火焰检测器，所述火焰检测器设在所述过渡导风筒内。The combustion processor according to any one of claims 31-35, further comprising a flame detector, the flame detector being provided in the transition air duct.
一种根据权利要求31-36中任一项所述的燃烧处理器的使用方法，其特征在于，包括以下步骤：A method of using a combustion processor according to any one of claims 31-36, characterized in that it comprises the following steps:

S1、将生物质粉和煤粉掺混(掺混比20％～100％)；S1. Blend biomass powder and coal powder (mixing ratio 20% to 100%);

S2、点燃点火器；S2, ignite the igniter;

S3、分两路通入空气，一路经助燃风通道进入稳燃腔，另一路经贴壁风通道进入稳燃腔；S3. Enter the air in two ways, one way enters the stable combustion chamber through the combustion-supporting air channel, and the other enters the stable combustion chamber through the wall-mounted air channel;

S4、将掺混后的生物质粉和煤粉经风粉管和回流帽组成的回流通道吹入稳燃腔内；S4, blowing the mixed biomass powder and coal powder into the stable combustion chamber through the return channel composed of the air powder pipe and the return cap;

S5、通过调温通道向稳燃腔内通入氧化性气体或惰性气体。S5, introducing oxidizing gas or inert gas into the combustion stabilization chamber through the temperature regulation channel.
根据权利要求37所述的燃烧处理器的使用方法，其特征在于，所述生物质粉和煤粉的粒径为50～250微米。The method for using a combustion processor according to claim 37, wherein the particle size of the biomass powder and coal powder is 50-250 microns.