CN111359570A - Annular reactor - Google Patents

Annular reactor Download PDF

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Publication number
CN111359570A
CN111359570A CN202010128577.6A CN202010128577A CN111359570A CN 111359570 A CN111359570 A CN 111359570A CN 202010128577 A CN202010128577 A CN 202010128577A CN 111359570 A CN111359570 A CN 111359570A
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heating
reactor according
ring
loop reactor
casing
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吴韬
杨刚
史楷岐
罗象
陈艺珮
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Nottingham Ningbo New Materials Institute Co ltd
University of Nottingham Ningbo China
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Nottingham Ningbo New Materials Institute Co ltd
University of Nottingham Ningbo China
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/18Stationary reactors having moving elements inside
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0006Controlling or regulating processes
    • B01J19/0013Controlling the temperature of the process
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0053Details of the reactor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J4/00Feed or outlet devices; Feed or outlet control devices
    • B01J4/001Feed or outlet devices as such, e.g. feeding tubes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/08Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • B01J8/085Feeding reactive fluids
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/08Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • B01J8/087Heating or cooling the reactor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/08Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
    • B01J8/10Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by stirrers or by rotary drums or rotary receptacles or endless belts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/00132Controlling the temperature using electric heating or cooling elements
    • B01J2219/00135Electric resistance heaters
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/00139Controlling the temperature using electromagnetic heating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/00139Controlling the temperature using electromagnetic heating
    • B01J2219/00141Microwaves
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049Controlling or regulating processes
    • B01J2219/00051Controlling the temperature
    • B01J2219/00139Controlling the temperature using electromagnetic heating
    • B01J2219/00146Infrared radiation

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

The invention provides an annular reactor, which comprises a shell, at least one heating source and a rotating part, wherein the shell is provided with a plurality of heating holes; the utility model discloses a heating source, including casing, rotating part, drive mechanism, feed inlet and discharge gate, the casing has the chamber of holding in, the heating source with casing fixed connection, rotating part is including putting thing ring sum actuating mechanism, it installs to put the thing ring it installs to hold the intracavity, actuating mechanism with it connects to put thing ring drive, the casing is equipped with feed inlet and discharge gate, follows put the rotation direction of thing ring, it follows to hold the chamber the regional zone of heating that is between feed inlet and the discharge gate, the heating source is arranged in the zone of heating. The invention has simple structure, reliable operation and good sealing performance, and can continuously and efficiently carry out reaction by rotating the object placing ring to convey materials.

Description

一种环形反应器a ring reactor

技术领域technical field

本发明涉及反应器技术领域,具体而言,涉及一种环形反应器。The present invention relates to the technical field of reactors, in particular, to a loop reactor.

背景技术Background technique

反应器是工业生产和实验研究常用的设备,现有的反应器具有多种形式,如釜式反应器、推进式反应器、传送带式反应器等。Reactors are commonly used equipment in industrial production and experimental research. Existing reactors have various forms, such as tank reactors, pusher reactors, conveyor belt reactors, and the like.

但现有的反应器都存在一些不足:如推进式反应器体积较大,会导致腔体内温度不均匀,物料受热不均,加热过程不易控制;釜式反应器需要批量生产,无法连续运行,且釜式反应器工作效率较低,反应时间长;传送带式反应器构造复杂,操作麻烦,且延伸区域大,不易密封,容易造成气体泄露。However, the existing reactors have some shortcomings: for example, the propellant reactor is large in size, which will lead to uneven temperature in the cavity, uneven heating of the material, and difficult to control the heating process; the kettle reactor requires batch production and cannot be operated continuously. In addition, the working efficiency of the kettle-type reactor is low, and the reaction time is long; the conveyor-type reactor has a complex structure, is troublesome to operate, and has a large extension area, which is not easy to seal, and easily causes gas leakage.

因此亟需一种新的反应器以满足连续生产的需要,提高生产效率,改善产物质量。Therefore, a new reactor is urgently needed to meet the needs of continuous production, improve production efficiency and improve product quality.

发明内容SUMMARY OF THE INVENTION

本发明解决的问题是如何改进反应器结构,实现连续反应,提高生产效率。The problem solved by the present invention is how to improve the reactor structure, realize continuous reaction and improve production efficiency.

为解决上述问题,本发明提供一种环形反应器,包括壳体、至少一个加热源和转动部件;所述壳体内具有容纳腔,所述加热源与所述壳体固定连接,所述转动部件包括置物环和驱动机构,所述置物环安装在所述容纳腔内,所述驱动机构与所述置物环驱动连接,所述壳体设有进料口和出料口,沿所述置物环的转动方向,所述容纳腔从所述进料口至所述出料口之间区域为加热区,所述加热源排列在所述加热区。In order to solve the above problems, the present invention provides an annular reactor, comprising a casing, at least one heating source and a rotating part; the casing has a accommodating cavity, the heating source is fixedly connected with the casing, and the rotating part It includes a storage ring and a driving mechanism, the storage ring is installed in the accommodating cavity, the driving mechanism is drivingly connected with the storage ring, and the shell is provided with a feeding port and a discharging port, along the storage ring In the direction of rotation, the area between the accommodating cavity from the feed port to the discharge port is a heating area, and the heating source is arranged in the heating area.

可选地,所述加热区呈扇环形,所述加热区的圆心角度数为180°-330°。Optionally, the heating zone is in the shape of a fan ring, and the central angle of the heating zone is 180°-330°.

可选地,所述加热源的数量为一个,所述加热源设置在所述壳体的上部、下部、外侧或内部。Optionally, the number of the heating source is one, and the heating source is arranged on the upper part, the lower part, the outer side or the inner part of the casing.

可选地,所述加热源的数量为两个或以上,多个所述加热源弧形排列在所述加热区,相邻所述加热源之间构成的圆弧的圆心角度数为15°-60°。Optionally, the number of the heating sources is two or more, a plurality of the heating sources are arranged in an arc in the heating zone, and the center angle of the arc formed between the adjacent heating sources is 15°. -60°.

可选地,所述加热源为微波发生器、红外发生器、电加热器或电磁感应加热器。Optionally, the heating source is a microwave generator, an infrared generator, an electric heater or an electromagnetic induction heater.

可选地,所述微波发生器为磁控管、固态微波源或光生微波源,发射频率为915MHz或2450MHz。Optionally, the microwave generator is a magnetron, a solid-state microwave source or a photo-generated microwave source, and the emission frequency is 915MHz or 2450MHz.

可选地,所述驱动机构包括驱动电机和传动件,所述驱动电机的输出轴穿过所述壳体的壁面与所述传动件连接,所述传动件与所述置物环驱动连接。Optionally, the driving mechanism includes a driving motor and a transmission member, an output shaft of the driving motor is connected to the transmission member through the wall surface of the housing, and the transmission member is drivingly connected to the storage ring.

可选地,所述传动件为齿轮、链条或皮带。Optionally, the transmission member is a gear, a chain or a belt.

可选地,所述容纳腔内设有至少一个搅拌板,所述搅拌板相对于所述置物环倾斜设置。Optionally, at least one stirring plate is provided in the accommodating cavity, and the stirring plate is inclined relative to the placing ring.

可选地,所述容纳腔内设有布料板,所述布料板设置在所述进料口位置,用于将从所述进料口进入所述容纳腔的物料铺设在所述置物环上。Optionally, a distribution board is arranged in the accommodating cavity, and the distribution board is arranged at the position of the feeding port, and is used for laying the material entering the accommodating cavity from the feeding port on the storage ring .

可选地,所述容纳腔内设有导向件,所述导向件设置在所述出料口位置,用于将所述置物环上的物料导向所述出料口。Optionally, a guide member is provided in the accommodating cavity, and the guide member is arranged at the position of the discharge port, and is used for guiding the material on the storage ring to the discharge port.

可选地,所述顶壁上设有排气管,所述排气管与所述容纳腔连通。Optionally, an exhaust pipe is provided on the top wall, and the exhaust pipe communicates with the accommodating cavity.

可选地,所述排气管的出口设有法兰。Optionally, the outlet of the exhaust pipe is provided with a flange.

可选地,环形反应器还包括进料部件,所述进料部件包括进料斗和螺旋进料机,所述进料斗与所述螺旋进料机的进口连接,所述螺旋进料机的出口与所述进料口连接。Optionally, the annular reactor further includes a feeding part, the feeding part includes a feeding hopper and a screw feeder, the feeding hopper is connected with the inlet of the screw feeder, and the screw feeder The outlet is connected with the feed port.

可选地,环形微波有机物质热解装置还包括出料部件,所述出料部件包括落料管与水冷器,所述落料管的两端分别与所述出料口和所述水冷器连接。Optionally, the annular microwave organic matter pyrolysis device further includes a discharge part, the discharge part includes a blanking pipe and a water cooler, and the two ends of the blanking pipe are respectively connected to the discharge port and the water cooler. connect.

相对于现有技术,本发明环形反应器结构简单,运行可靠,密封性好,通过置物环转动传输物料,能够连续、高效地进行反应;在加热区设置加热源,保证加热区内升温迅速,加热均匀,提高产品品质;容纳腔内设置搅拌板,对物料进行搅拌,提高传热速率,促进反应进行;进料口位置设置布料板,使铺设在置物环上的物料厚度均匀,保证产物的一致性;出料口设置导向件,不仅可以将产物导入出料口,还可以对置物环表面进行清洁,避免物料残留。Compared with the prior art, the annular reactor of the present invention has the advantages of simple structure, reliable operation and good sealing performance, and can continuously and efficiently carry out the reaction through the rotation of the placing ring to transmit the material; the heating source is arranged in the heating zone to ensure that the temperature rises rapidly in the heating zone, The heating is uniform and the product quality is improved; a stirring plate is set in the holding chamber to stir the material, improve the heat transfer rate, and promote the reaction; a distributing plate is set at the position of the feeding port, so that the thickness of the material laid on the storage ring is uniform, and the product is guaranteed. Consistency; the discharge port is provided with a guide, which can not only guide the product into the discharge port, but also clean the surface of the placing ring to avoid material residues.

附图说明Description of drawings

图1为本发明实施例中环形反应器的局部透视俯视图;1 is a partial perspective top view of an annular reactor in an embodiment of the present invention;

图2为本发明实施例中环形反应器的剖视图;Fig. 2 is the sectional view of the annular reactor in the embodiment of the present invention;

图3为本发明另一实施例中环形反应器的剖视图;Figure 3 is a cross-sectional view of an annular reactor in another embodiment of the present invention;

图4为图3中A处的局部放大图;Fig. 4 is the partial enlarged view of A place in Fig. 3;

图5为本发明另一实施例中环形反应器的局部透视俯视图;5 is a partial perspective top view of an annular reactor in another embodiment of the present invention;

图6为本发明另一实施例中环形反应器的剖视图一;6 is a cross-sectional view one of the annular reactor in another embodiment of the present invention;

图7为本发明另一实施例中环形反应器的剖视图二;Fig. 7 is the cross-sectional view 2 of the annular reactor in another embodiment of the present invention;

图8为本发明另一实施例中环形反应器的剖视图三。FIG. 8 is a cross-sectional view 3 of the annular reactor in another embodiment of the present invention.

附图标记说明:Description of reference numbers:

11-壳体,12-顶壁,13-锁紧轮,14-容纳腔,15-操作平台,16-进料口,17-出料口,2-微波发生器,31-置物环,32-驱动电机,33-齿轮,34-链条,35-链轮,311-底板,312-侧板,313-翻边,41-出料挡板,42-搅拌板,43-布料板,5-排气管,61-进料斗,62-螺旋进料机,71-落料管,72-水冷器,73-接料箱。11-shell, 12-top wall, 13-locking wheel, 14-accommodating cavity, 15-operating platform, 16-feeding port, 17-feeding port, 2-microwave generator, 31- storage ring, 32 -Drive motor, 33-gear, 34-chain, 35-sprocket, 311-bottom plate, 312-side plate, 313-flanging, 41-discharge baffle, 42-stirring plate, 43-distribution plate, 5- Exhaust pipe, 61-feed hopper, 62-screw feeder, 71-blanking pipe, 72-water cooler, 73- receiving box.

具体实施方式Detailed ways

在本发明的描述中,应当说明的是,各实施例中的术语名词例如“上”、“下”、“前”、“后”、“左”、“右”等指示方位的词语,只是为了简化描述基于说明书附图的位置关系,并不代表所指的元件和装置等必须按照说明书中特定的方位和限定的操作及方法、构造进行操作,该类方位名词不构成对本发明的限制。In the description of the present invention, it should be noted that the terms and nouns in the various embodiments, such as "upper", "lower", "front", "rear", "left", "right" and other words indicating orientation, only In order to simplify the description based on the positional relationship of the drawings in the description, it does not mean that the elements and devices referred to must be operated according to the specific orientation and limited operations, methods and structures in the description, and such orientation terms do not limit the present invention.

本发明的实施例的附图中设置有坐标系XYZ,其中X的正向代表前方,X的反向代表后方,Y轴的正向代表上方,Y轴的反向代表下方,Z轴的正向代表右方,Z轴的反向代表左方。The drawings of the embodiments of the present invention are provided with a coordinate system XYZ, wherein the positive direction of X represents the front, the reverse direction of X represents the rear, the positive direction of the Y axis represents the upper direction, the reverse direction of the Y axis represents the downward direction, and the positive direction of the Z axis represents the downward direction. The direction represents the right, and the reverse of the Z axis represents the left.

为使本发明的上述目的、特征和优点能够更为明显易懂,下面结合附图对本发明的具体实施例做详细的说明。In order to make the above objects, features and advantages of the present invention more clearly understood, the specific embodiments of the present invention will be described in detail below with reference to the accompanying drawings.

结合图1和图2所示,本实施例提供过一种环形反应器,可以用于热解反应、气化反应、碳化、冶金、干燥、废弃物处理等用途。1 and 2, this embodiment provides an annular reactor, which can be used for pyrolysis reaction, gasification reaction, carbonization, metallurgy, drying, waste treatment and other purposes.

环形反应器包括装配在一起的壳体11、转动部件、进料部件和出料部件。壳体11整体为圆环体形,其具有圆环体形的容纳腔14,壳体11具有两个侧壁,内侧壁面为壳体11的内侧壁,外侧壁面为壳体11的外侧壁,物料在容纳腔14中完成反应。The annular reactor comprises a shell 11, a rotating part, a feed part and a discharge part assembled together. The casing 11 is in the shape of a torus as a whole, and has a torus-shaped accommodating cavity 14. The casing 11 has two side walls. The reaction is completed in the holding chamber 14 .

本实施例中,壳体11的顶壁12上设有多个加热源。在其他实施方式中,加热源的数量可以为一个或以上,加热源可以设置在壳体11的上部、下部或外侧,通过馈入壳体11的方式加热,也可以直接设置在壳体11内部。环形反应器可以用于固体样品、液体样品反应,也可以在容纳腔14内投入催化剂进行气体反应,加热源用于对容纳腔14内物料进行加热。In this embodiment, a plurality of heating sources are provided on the top wall 12 of the casing 11 . In other embodiments, the number of heating sources may be one or more, and the heating sources may be arranged on the upper, lower or outer sides of the housing 11 , and the heating sources may be heated by feeding into the housing 11 , or they may be directly arranged inside the housing 11 . . The annular reactor can be used for the reaction of solid samples and liquid samples, or a catalyst can be put into the accommodating chamber 14 for gas reaction, and the heating source is used to heat the materials in the accommodating chamber 14 .

本实施例中,加热源为微波发生器2。在其他实施方式中,加热源可以选用红外发生器、电加热器、电磁感应加热器等。In this embodiment, the heating source is the microwave generator 2 . In other embodiments, the heating source may be an infrared generator, an electric heater, an electromagnetic induction heater, or the like.

环形反应器壳体11的顶壁12可拆卸,便于对容纳腔14进行清理。在壳体11的内侧壁和外侧壁上都设置多组用于固定顶壁12的锁紧轮13,一组锁紧轮13为两个,分别设置在内侧壁和外侧壁相对应的位置。锁紧轮13可以用手或撬棍锁定和打开,操作方便。锁紧轮13至少为三组,各组锁紧轮13均匀分布,保证顶壁12各部位受力均匀,连接可靠。可以在顶壁12下方设置密封垫,通过锁紧轮13使顶壁12与壳体11其他部位相互压紧,保证壳体11的密封性。The top wall 12 of the annular reactor shell 11 is detachable to facilitate cleaning of the accommodating cavity 14 . Multiple sets of locking wheels 13 for fixing the top wall 12 are provided on both the inner and outer side walls of the housing 11 , and a set of two locking wheels 13 are respectively arranged at corresponding positions on the inner and outer side walls. The locking wheel 13 can be locked and opened by hand or a crowbar, which is convenient to operate. There are at least three groups of locking wheels 13 , and the locking wheels 13 of each group are evenly distributed to ensure that all parts of the top wall 12 are uniformly stressed and connected reliably. A sealing gasket may be provided under the top wall 12 , and the top wall 12 and other parts of the casing 11 are pressed against each other by the locking wheel 13 to ensure the sealing of the casing 11 .

顶壁12上设有进料口16,进料部件包括进料斗61和螺旋进料机62,进料斗61与螺旋进料机62的进口连接,螺旋进料机62的出口与进料口16连接。进料斗61具有一定的盛料空间,待反应的物料经过螺旋进料机62粉碎后送入容纳腔14,螺旋进料机62可以连续送料。The top wall 12 is provided with a feeding port 16. The feeding component includes a feeding hopper 61 and a screw feeder 62. The feeding hopper 61 is connected to the inlet of the screw feeder 62, and the outlet of the screw feeder 62 is connected to the feeder. Port 16 is connected. The feeding hopper 61 has a certain material holding space, and the material to be reacted is crushed by the screw feeder 62 and sent into the accommodating cavity 14, and the screw feeder 62 can continuously feed the material.

壳体11上设有出料口17,本实施例中出料口17设置在内侧壁上,出料部件包括落料管71与水冷器72,落料管71的两端分别与出料口17和水冷器72连接,物料在容纳腔14内完成反应后从出料口17送出,反应后得到的产物经过落料管71进入水冷器72进行冷却降温,便于产物收集。在其他实施方式中,出料口17可以设置在壳体11的外侧壁或底部,便于安装体积较大的出料部件。The shell 11 is provided with a discharge port 17. In this embodiment, the discharge port 17 is arranged on the inner side wall. The discharge components include a blanking pipe 71 and a water cooler 72. The two ends of the blanking pipe 71 are respectively connected to the discharge port. 17 is connected to the water cooler 72, the material is sent out from the discharge port 17 after the reaction is completed in the accommodating chamber 14, and the product obtained after the reaction enters the water cooler 72 through the blanking pipe 71 for cooling and cooling, which is convenient for product collection. In other embodiments, the discharge port 17 may be disposed on the outer side wall or the bottom of the housing 11 to facilitate the installation of large volume discharge components.

所述转动部件包括置物环31和驱动机构,驱动机构包括驱动电机32和传动件,本实施例中传动件为齿轮33,在其他实施方式中,传动件还可以是链条或皮带等。驱动电机32的输出轴穿过外侧壁与齿轮33连接,用于控制齿轮33转动。The rotating component includes a storage ring 31 and a driving mechanism, and the driving mechanism includes a driving motor 32 and a transmission member. In this embodiment, the transmission member is a gear 33. In other embodiments, the transmission member can also be a chain or a belt. The output shaft of the driving motor 32 is connected to the gear 33 through the outer side wall, and is used to control the rotation of the gear 33 .

本实施例中驱动电机32和齿轮33的数量为四个,均匀布置在壳体11上。齿轮33和置物环31安装在容纳腔14内,置物环31架设在齿轮33上,齿轮33可以驱动置物环31转动,置物环31可以单独取下清理或更换,节省维护成本。在其他实施方式中,驱动电机32和齿轮33的数量可以为2-12个,驱动电机32和齿轮33的数量增加,可以使置物环31转动更加平稳。物料从进料口16进入容纳腔14后落在置物环31上,驱动电机32控制齿轮33转动,置物环31跟随转动,使物料在容纳腔14内传送,微波发生器2发出微波对物料进行加热,反应完成后物料从出料口17送出。In this embodiment, the number of the driving motors 32 and the gears 33 is four, which are evenly arranged on the casing 11 . The gear 33 and the storage ring 31 are installed in the accommodating cavity 14, the storage ring 31 is erected on the gear 33, the gear 33 can drive the storage ring 31 to rotate, and the storage ring 31 can be removed separately for cleaning or replacement, saving maintenance costs. In other embodiments, the number of driving motors 32 and gears 33 may be 2-12, and the increase in the number of driving motors 32 and gears 33 can make the rotation of the storage ring 31 more stable. The material enters the accommodating cavity 14 from the feeding port 16 and then falls on the storage ring 31. The drive motor 32 controls the rotation of the gear 33, and the storage ring 31 rotates accordingly, so that the material is transported in the accommodating cavity 14, and the microwave generator 2 emits microwaves to carry out the material processing. After heating, the material is sent out from the discharge port 17 after the reaction is completed.

较佳地,置物环31表面与齿轮33接触部位为齿面结构,齿轮33的轮齿与置物环31表面啮合,保证传动可靠。Preferably, the contact part between the surface of the storage ring 31 and the gear 33 is a tooth surface structure, and the teeth of the gear 33 mesh with the surface of the storage ring 31 to ensure reliable transmission.

顶壁12上设有排气管5,其与容纳腔14连通,用于排出反应产生的气体,避免容纳腔14内压力升高。排气管5靠近出料口17位置,随着反应进行,产生的气体增加,排气管5与出料口17接近可以尽快排出反应产生的气体,防止憋压。The top wall 12 is provided with an exhaust pipe 5 , which communicates with the accommodating cavity 14 and is used to discharge the gas produced by the reaction, so as to prevent the pressure in the accommodating cavity 14 from rising. The exhaust pipe 5 is close to the discharge port 17. As the reaction progresses, the generated gas increases. The exhaust pipe 5 is close to the discharge port 17 so that the gas generated by the reaction can be discharged as soon as possible to prevent the pressure from being held back.

较佳地,排气管5的出口设有法兰,当需要在密封状态下进入反应时,可以用法兰封闭排气管5,操作方便。Preferably, the outlet of the exhaust pipe 5 is provided with a flange. When it is necessary to enter the reaction in a sealed state, the exhaust pipe 5 can be sealed with a flange, which is convenient to operate.

在出料口17位置设有导向件,用于将置物环31上的物料导向出料口17。本实施例中,容纳腔4用于固体反应,出料口17设置在壳体11的内侧壁上,导向件为出料挡板41。出料挡板41的水平截面为弧形,沿置物盘转动方向,从容纳腔14外侧向内侧倾斜。置物环31转动,将反应后的物料输送到出料口17附近时会被出料挡板41挡住,被挡住的物料沿出料挡板41滑向出料口17,进入出料部件。出料挡板41为倾斜设置的弧形板,利于物料沿出料挡板41进入出料口17,防止产物堆积在出料挡板41。出料挡板41与壳体11内侧壁或顶壁12连接,出料挡板41的底部与置物环31的底板311表面贴合,置物环31转动时使出料挡板41扫过置物环31的表面,避免反应后的产物残留在置物环31上。A guide member is provided at the position of the discharge port 17 for guiding the material on the storage ring 31 to the discharge port 17 . In this embodiment, the accommodating chamber 4 is used for solid reaction, the discharge port 17 is arranged on the inner side wall of the casing 11 , and the guide member is the discharge baffle 41 . The horizontal section of the discharge baffle 41 is arc-shaped, and is inclined from the outside to the inside of the accommodating cavity 14 along the rotation direction of the storage tray. When the storage ring 31 rotates, the reacted material will be blocked by the discharge baffle 41 when it is transported to the vicinity of the discharge port 17, and the blocked material slides along the discharge baffle 41 to the discharge port 17 and enters the discharge part. The discharge baffle 41 is an inclined arc-shaped plate, which facilitates the material entering the discharge port 17 along the discharge baffle 41 and prevents the products from accumulating on the discharge baffle 41 . The discharge baffle 41 is connected to the inner side wall or the top wall 12 of the housing 11 , the bottom of the discharge baffle 41 is in contact with the surface of the bottom plate 311 of the storage ring 31 , and the discharge baffle 41 sweeps over the storage ring when the storage ring 31 rotates 31 to prevent the reacted product from remaining on the placement ring 31.

在其他实施方式中,当容纳腔4用于液体反应时,导向件为出料流道;当容纳腔4用于气体反应时,导向件为气体导管。In other embodiments, when the accommodating chamber 4 is used for liquid reaction, the guide member is the outflow channel; when the accommodating chamber 4 is used for gas reaction, the guide member is a gas conduit.

结合图1所示,为了节省反应装置的制造成本,仅需要对物料经过的容纳腔14部位进行加热,在需加热的容纳腔14部位设置加热源即可。定义物料在传送过程中经过的区域为加热区,即沿置物环31的转动方向,容纳腔14从进料口16至出料口17之间区域。Referring to FIG. 1 , in order to save the manufacturing cost of the reaction device, it is only necessary to heat the part of the accommodating cavity 14 through which the material passes, and a heating source can be provided in the part of the accommodating cavity 14 to be heated. The area that the material passes through during the conveying process is defined as the heating area, that is, the area between the accommodating cavity 14 from the feed port 16 to the discharge port 17 along the rotation direction of the storage ring 31 .

本实施例中加热区呈扇环形,加热区的圆心角度数为300°。加热源数量为7个,呈弧形排列在加热区的上方。各个加热源之间的间隔距离相同,保证加热区内温度均匀,相邻加热源之间构成的圆弧的圆心角度数为40°。In this embodiment, the heating zone is in the shape of a fan ring, and the central angle of the heating zone is 300°. The number of heating sources is 7, which are arranged in an arc above the heating zone. The distance between each heating source is the same to ensure uniform temperature in the heating area, and the number of center angles of the arc formed between adjacent heating sources is 40°.

进一步地,加热源为微波发生器2,微波发生器2可以选择磁控管、固态微波源或光生微波源,其频率为915MHz或2450MHz,具有很高的加热效率,能使物料快速反应。Further, the heating source is a microwave generator 2. The microwave generator 2 can be selected from a magnetron, a solid-state microwave source or a photogenerated microwave source.

进一步地,在容纳腔14内设置4个搅拌板42,其均匀分布在加热区内。搅拌板42为相对于置物环31倾斜设置斜板,搅拌板42与壳体11的内侧壁连接。置物环31转动过程中,物料会经过搅拌板42,对物料进行搅拌混合,提高传热速率,促进反应进行。在其他实施方式中,搅拌板42的数量为1-12个,搅拌板42可以与壳体11连接,也可以与顶壁12连接。Further, four stirring plates 42 are arranged in the accommodating cavity 14 and are evenly distributed in the heating area. The stirring plate 42 is an inclined plate inclined relative to the storage ring 31 , and the stirring plate 42 is connected to the inner side wall of the housing 11 . During the rotation of the placing ring 31 , the material will pass through the stirring plate 42 to agitate and mix the material, thereby increasing the heat transfer rate and promoting the reaction. In other embodiments, the number of stirring plates 42 is 1-12, and the stirring plates 42 can be connected with the housing 11 or with the top wall 12 .

本实施例公开的环形反应器的工作流程如下:The workflow of the loop reactor disclosed in the present embodiment is as follows:

使用者将原料投入进料斗61,保持进料斗61中始终有物料,螺旋进料机62将原料粉碎后从进料口16送入容纳腔14;The user puts the raw material into the feeding hopper 61, and keeps the material in the feeding hopper 61 at all times, and the screw feeder 62 pulverizes the raw material and sends it into the accommodating cavity 14 from the feeding port 16;

粉碎的物料落在置物环31上,驱动电机32控制齿轮33转动,通过齿轮33传动使置物环31跟随转动,物料沿置物环31转动方向从进料口16向出料口17传送,微波发生器2发出微波加热容纳腔14内的物料,物料在从进料口16至出料口17的传送过程中完成反应,得到反应产物;The crushed material falls on the storage ring 31, the drive motor 32 controls the gear 33 to rotate, and the gear 33 drives the storage ring 31 to follow the rotation. The device 2 emits microwaves to heat the material in the accommodating cavity 14, and the material completes the reaction during the transmission process from the feed port 16 to the discharge port 17 to obtain a reaction product;

产物碰到出料挡板41,沿出料挡板41进入出料口17,产物离开容纳腔14进入落料管71,再进入水冷器72被降温,使用者收集降温后的产物。The product hits the discharge baffle 41 and enters the discharge port 17 along the discharge baffle 41. The product leaves the accommodation cavity 14 and enters the blanking pipe 71, and then enters the water cooler 72 to be cooled. The user collects the cooled product.

本实施例中环形反应器的置物环31可以持续转动进行物料传输,使用者向进料部件连续投料,通过微波发生器2加热可以高效完成反应,出料部件会持续得到产物,实现连续作业,提高工作效率。In this embodiment, the storage ring 31 of the annular reactor can be continuously rotated for material transmission. The user continuously feeds materials to the feeding part, and the reaction can be efficiently completed by heating by the microwave generator 2; Improve work efficiency.

本实施例在上述实施例的基础上,对环形反应器的参数进行限定。其中,加热区的圆心角度数θ为0°-360°,根据实际情况设置,加热区不宜过小,否则会造成装置效率不足,也不宜过大,否则进料口16与出料口17之间距离太近,进料口16的原料与反应后的产物容易混合在一起。置物环31的外径D为5m-20m,使反应器体积不要过大,便于移动和维护。置物环31的转速R为0.01-0.1rpm,在保证反应能够完成的基础上提高工作效率。加热源的最高功率W为200w-800w,反应器使用过程中,加热源的实际工作功率从零到最高功率之间可调,可以适用于不同的物料。加热源的数量n为1-22个,相邻加热源之间构成的圆弧的圆心角度数α为15°-60°,加热源均匀分布在加热区,各加热源之间的间隔相等,保证加热区内温度均匀,产物可预测性高。加热源的最高功率和数量可以根据反应器的其他部件参数进行选择,保证装置能够高效连续运行。In this embodiment, the parameters of the annular reactor are limited on the basis of the above-mentioned embodiment. Among them, the number θ of the center angle of the heating zone is 0°-360°. It should be set according to the actual situation. The heating zone should not be too small, otherwise the device efficiency will be insufficient, and it should not be too large. If the distance is too close, the raw material of the feed port 16 and the reacted product are easily mixed together. The outer diameter D of the placement ring 31 is 5m-20m, so that the volume of the reactor should not be too large, which is convenient for movement and maintenance. The rotational speed R of the placement ring 31 is 0.01-0.1 rpm, which improves the work efficiency on the basis of ensuring that the reaction can be completed. The maximum power W of the heating source is 200w-800w. During the use of the reactor, the actual working power of the heating source can be adjusted from zero to the highest power, which can be applied to different materials. The number n of heating sources is 1-22, the central angle α of the arc formed between adjacent heating sources is 15°-60°, the heating sources are evenly distributed in the heating area, and the intervals between the heating sources are equal. Ensure uniform temperature in the heating zone and high product predictability. The maximum power and number of heating sources can be selected according to the parameters of other components of the reactor to ensure that the device can operate efficiently and continuously.

进一步地,可以根据物料反应所需要的能量,选定环形反应器的参数,反应器的各项参数需要满足以下公式:Further, the parameters of the annular reactor can be selected according to the energy required for the reaction of the material, and the parameters of the reactor need to meet the following formulas:

Figure BDA0002395170780000071
Figure BDA0002395170780000071

其中,E为能量设定值,根据环形反应器所需处理的物料预先设定;W为加热源的最高功率;θ为加热区的圆心角度数;α为相邻加热源之间构成的圆弧的圆心角度数,加热源的数量至少为2个;D为置物环的外径;R为置物环的转速。Among them, E is the energy setting value, which is preset according to the materials to be processed in the annular reactor; W is the maximum power of the heating source; θ is the central angle of the heating zone; α is the circle formed between adjacent heating sources. The number of the center angle of the arc, and the number of heating sources is at least 2; D is the outer diameter of the placement ring; R is the rotational speed of the placement ring.

根据该公式选择合适的装置参数,保证物料可以在容纳腔14内完成反应,实现高效连续作业。实际使用时加热源的功率可以在最大值范围内调节,适用于不用的物料,通用性更好。Appropriate device parameters are selected according to the formula to ensure that the material can complete the reaction in the accommodating chamber 14 and realize efficient and continuous operation. In actual use, the power of the heating source can be adjusted within the maximum value range, which is suitable for unused materials and has better versatility.

结合图3和图4所示,本实施例提供另一种环形反应器,包括装配在一起的壳体11、顶壁12、转动部件、进料部件和出料部件。壳体11具有圆环体形的凹槽,凹槽顶部开口,顶壁12设置在壳体11的顶部,通过锁紧轮13固定,壳体11和顶壁12之间的空间构成容纳腔14。顶壁12上设有进料口16,进料部件包括进料斗61和螺旋进料机62,进料斗61与螺旋进料机62的进口连接,螺旋进料机62的出口与进料口16连接。在壳体11的右侧设置操作平台15,操作平台15的高度与进料斗61高度接近,便于使用者将物料投入进料斗61。壳体11上设有出料口17,在出料口17位置设有出料挡板41,用于将置物环31上的物料导向出料口17。出料部件包括落料管71与水冷器72,落料管71的两端分别与出料口17和水冷器72连接。转动部件包括置物环31、驱动电机32和齿轮33。驱动电机32与齿轮33连接,用于控制齿轮33转动。3 and 4, this embodiment provides another annular reactor, which includes a shell 11, a top wall 12, a rotating part, a feeding part and a discharging part assembled together. The casing 11 has a circular groove with an open top. The top wall 12 is arranged on the top of the casing 11 and is fixed by a locking wheel 13 . The space between the casing 11 and the top wall 12 constitutes an accommodation cavity 14 . The top wall 12 is provided with a feeding port 16. The feeding component includes a feeding hopper 61 and a screw feeder 62. The feeding hopper 61 is connected to the inlet of the screw feeder 62, and the outlet of the screw feeder 62 is connected to the feeder. Port 16 is connected. An operation platform 15 is provided on the right side of the housing 11 , and the height of the operation platform 15 is close to the height of the feeding hopper 61 , which is convenient for the user to put materials into the feeding hopper 61 . The casing 11 is provided with a discharge port 17 , and a discharge baffle 41 is provided at the position of the discharge port 17 for guiding the material on the storage ring 31 to the discharge port 17 . The discharging part includes a blanking pipe 71 and a water cooler 72 , and both ends of the blanking pipe 71 are respectively connected to the discharging port 17 and the water cooler 72 . The rotating parts include the storage ring 31 , the driving motor 32 and the gear 33 . The driving motor 32 is connected with the gear 33 for controlling the rotation of the gear 33 .

置物环31包括相互连接的底板311、侧板312和翻边313。底板311为水平设置的圆环板,底板311的内侧与壳体11的内侧壁贴合,防止物料从置物环31内侧漏出。底板311的外沿向上延伸形成侧板312,侧板312的上沿与顶壁12接近,侧板312竖直设置,用于阻挡物料从置物环31外侧漏出。侧板312的上沿向外侧延伸形成翻边313,翻边313水平设置。齿轮33竖直设置在翻边313的下方并与翻边313接触,齿轮33转动时推动翻边313移动,使置物环31发生转动。在其他实施方式中,齿轮33可以水平设置在侧板312的外侧,与侧板312接触,通过推动侧板312使置物环31转动;齿轮33还可以竖直设置在底板311下方,与底板311接触,通过推动底板311使置物环31转动。The storage ring 31 includes a bottom plate 311 , a side plate 312 and a flange 313 which are connected to each other. The bottom plate 311 is a horizontal annular plate, and the inner side of the bottom plate 311 is fitted with the inner side wall of the housing 11 to prevent the material from leaking from the inner side of the storage ring 31 . The outer edge of the bottom plate 311 extends upward to form a side plate 312 , and the upper edge of the side plate 312 is close to the top wall 12 . The upper edge of the side plate 312 extends outward to form a flange 313, and the flange 313 is arranged horizontally. The gear 33 is vertically arranged below the flange 313 and is in contact with the flange 313. When the gear 33 rotates, the flange 313 is pushed to move, so that the storage ring 31 rotates. In other embodiments, the gear 33 can be horizontally arranged on the outer side of the side plate 312 , in contact with the side plate 312 , and the storage ring 31 can be rotated by pushing the side plate 312 ; Contact, the storage ring 31 is rotated by pushing the bottom plate 311 .

沿置物环31的转动方向,容纳腔14从进料口16至出料口17之间区域为加热区,加热区的圆心角度数为280°。顶壁12上设有9个加热源,加热源为微波发生器2,呈弧形排列在加热区的上方。呈弧形排列在加热区的上方。各个微波发生器2之间的间隔距离相同,保证加热区内温度均匀,相邻微波发生器2之间构成的圆弧的圆心角度数为30°。在容纳腔14内设置3个搅拌板42,其均匀分布在加热区内,用于搅拌物料,提高传热速率,促进反应进行。Along the rotation direction of the storage ring 31 , the area between the feeding port 16 and the discharging port 17 of the accommodating cavity 14 is a heating zone, and the central angle of the heating zone is 280°. Nine heating sources are arranged on the top wall 12, and the heating sources are microwave generators 2, which are arranged above the heating zone in an arc shape. Arranged in an arc above the heating zone. The distances between the microwave generators 2 are the same to ensure uniform temperature in the heating area, and the center angle of the arc formed between adjacent microwave generators 2 is 30°. Three stirring plates 42 are arranged in the accommodating cavity 14, which are evenly distributed in the heating zone, and are used for stirring the materials, increasing the heat transfer rate, and promoting the reaction.

本实施例提供的环形反应器具有结构简单、运行可靠、密封性好、加热效率高、可连续化生产等诸多优点,具有很好的应用价值和市场推广前景。The annular reactor provided in this embodiment has many advantages, such as simple structure, reliable operation, good sealing performance, high heating efficiency, continuous production, etc., and has good application value and market promotion prospect.

结合图5至图8所示,本实施例提供另一种环形反应器,可以用于固体、液体和气体的热解反应、碳化、冶金、干燥等用途。环形反应器包括装配在一起的壳体11、转动部件、进料部件和出料部件。壳体11整体为圆环体形,其具有圆环体形的容纳腔14,壳体11具有两个侧壁,内侧壁面为壳体11的内侧壁,外侧壁面为壳体11的外侧壁,物料在容纳腔14中完成反应。壳体11的顶壁12上设有至少一个加热源,本实施例中加热源为微波发生器2,在其他实施方式中,加热源还可以用红外发生器、电加热器等替换。加热源安装在容纳腔14的上部,用于发出微波对容纳腔14内物料进行加热。With reference to FIGS. 5 to 8 , this embodiment provides another annular reactor, which can be used for pyrolysis, carbonization, metallurgy, and drying of solids, liquids, and gases. The annular reactor comprises a shell 11, a rotating part, a feed part and a discharge part assembled together. The casing 11 is in the shape of a torus as a whole, and has a torus-shaped accommodating cavity 14. The casing 11 has two side walls. The reaction is completed in the holding chamber 14 . The top wall 12 of the housing 11 is provided with at least one heating source. In this embodiment, the heating source is the microwave generator 2. In other embodiments, the heating source can also be replaced by an infrared generator, an electric heater, or the like. The heating source is installed on the upper part of the accommodating cavity 14 for emitting microwaves to heat the materials in the accommodating cavity 14 .

顶壁12可拆卸,便于对容纳腔14进行清理。在壳体11的外侧壁上都设置多个用于固定顶壁12的锁紧轮13。锁紧轮13可以用手或撬棍锁定和打开,操作方便。各个锁紧轮13均匀分布,保证顶壁12各部位受力均匀,连接可靠。The top wall 12 is detachable to facilitate cleaning of the accommodating cavity 14 . A plurality of locking wheels 13 for fixing the top wall 12 are arranged on the outer side wall of the housing 11 . The locking wheel 13 can be locked and opened by hand or a crowbar, which is convenient to operate. The locking wheels 13 are evenly distributed to ensure that all parts of the top wall 12 are uniformly stressed and connected reliably.

顶壁12上设有进料口16,进料部件包括进料斗61和螺旋进料机62,进料斗61与螺旋进料机62的进口连接,螺旋进料机62的出口与进料口16连接。The top wall 12 is provided with a feeding port 16. The feeding component includes a feeding hopper 61 and a screw feeder 62. The feeding hopper 61 is connected to the inlet of the screw feeder 62, and the outlet of the screw feeder 62 is connected to the feeder. Port 16 is connected.

壳体11上设有出料口17,本实施例中出料口17设置在外侧壁上。出料部件包括落料管71、水冷器72和接料箱73,落料管71的两端分别与出料口17和水冷器72连接,接料箱73设置在水冷器72出口的下方,用于收集降温后的产物。The casing 11 is provided with a discharge port 17, and in this embodiment, the discharge port 17 is provided on the outer side wall. The discharge part includes a blanking pipe 71, a water cooler 72 and a material receiving box 73. The two ends of the blanking pipe 71 are respectively connected with the discharge port 17 and the water cooler 72. The material receiving box 73 is arranged below the outlet of the water cooler 72, Used to collect the cooled product.

转动部件包括置物环31和驱动机构,驱动机构包括驱动电机32和传动件,本实施例中传动件为链条34。驱动电机32的输出轴穿过壳体11的底壁与链轮35连接,链轮34上设置链条34,驱动电机32可以驱动链条34传输。置物环31架设在链条34上,链条34可以驱动置物环31转动。The rotating part includes a storage ring 31 and a driving mechanism. The driving mechanism includes a driving motor 32 and a transmission member. In this embodiment, the transmission member is a chain 34 . The output shaft of the drive motor 32 is connected to the sprocket 35 through the bottom wall of the housing 11 , the chain 34 is provided on the sprocket 34 , and the drive motor 32 can drive the chain 34 to transmit. The storage ring 31 is mounted on the chain 34, and the chain 34 can drive the storage ring 31 to rotate.

在进料口16位置设有布料板43,用于将从进料口16进入容纳腔14的物料铺设在置物环31上。布料板43底部与置物环31表面距离固定,使铺设在置物环31上的物料厚度均匀,保证产物的一致性。在出料口17位置设有出料挡板41,用于将置物环31上的物料导向出料口17。出料口17设置在壳体11的外侧壁上,出料挡板41的水平截面直线,沿置物盘转动方向,从容纳腔14内侧向外侧倾斜。置物环31转动,将反应后的物料输送到出料口17附近时会被出料挡板41挡住,被挡住的物料沿出料挡板41滑向出料口17,进入出料部件。A distribution board 43 is provided at the position of the feed port 16 for laying the material entering the accommodating cavity 14 from the feed port 16 on the storage ring 31 . The distance between the bottom of the cloth plate 43 and the surface of the storage ring 31 is fixed, so that the thickness of the material laid on the storage ring 31 is uniform and the consistency of the product is ensured. A discharge baffle 41 is provided at the position of the discharge port 17 for guiding the material on the storage ring 31 to the discharge port 17 . The discharge port 17 is arranged on the outer side wall of the casing 11 , and the horizontal cross-section of the discharge baffle 41 is straight and inclined from the inner side of the accommodating cavity 14 to the outer side along the rotation direction of the storage tray. When the storage ring 31 rotates, the reacted material will be blocked by the discharge baffle 41 when it is transported to the vicinity of the discharge port 17, and the blocked material slides along the discharge baffle 41 to the discharge port 17 and enters the discharge part.

定义物料在传送过程中经过的区域为加热区,即沿置物环31的转动方向,容纳腔14从进料口16至出料口17之间区域。结合图8所示,本实施例中加热区呈扇环形,加热区的圆心角度数为270°。加热源数量为12个,呈弧形排列在加热区的上方。各个加热源之间的间隔距离相同,保证加热区内温度均匀,相邻加热源之间构成的圆弧的圆心角度数为22.5°。The area that the material passes through during the conveying process is defined as the heating area, that is, the area between the accommodating cavity 14 from the feed port 16 to the discharge port 17 along the rotation direction of the storage ring 31 . Referring to FIG. 8 , in this embodiment, the heating zone is in a fan-shaped ring shape, and the central angle of the heating zone is 270°. The number of heating sources is 12, which are arranged in an arc above the heating zone. The distance between each heating source is the same to ensure uniform temperature in the heating area, and the center angle of the arc formed between adjacent heating sources is 22.5°.

本实施例中环形反应器的工作流程如下:The workflow of the loop reactor in the present embodiment is as follows:

使用者将原料投入进料斗61,保持进料斗61中始终有物料,螺旋进料机62将原料粉碎后从进料口16送入容纳腔14;The user puts the raw material into the feeding hopper 61, and keeps the material in the feeding hopper 61 at all times, and the screw feeder 62 pulverizes the raw material and sends it into the accommodating cavity 14 from the feeding port 16;

粉碎的物料落在置物环31上,驱动电机32控制链轮35转动,进而控制链条34和置物环31转动。布料板43将从进料口16进入容纳腔14的物料铺设在置物环31上,置物环31上的物料厚度均匀;The pulverized material falls on the storage ring 31 , and the driving motor 32 controls the rotation of the sprocket 35 , which in turn controls the rotation of the chain 34 and the storage ring 31 . The distribution board 43 lays the material entering the accommodating cavity 14 from the feeding port 16 on the storage ring 31, and the thickness of the material on the storage ring 31 is uniform;

物料沿置物环31转动方向从进料口16向出料口17传送,加热源发热,使容纳腔14内的物料反应,物料在从进料口16至出料口17的传送过程中完成反应,得到反应产物;The material is conveyed from the feed port 16 to the discharge port 17 along the rotation direction of the storage ring 31, and the heating source generates heat to make the material in the accommodating chamber 14 react. , to obtain the reaction product;

产物碰到出料挡板41,沿出料挡板41进入出料口17,产物离开容纳腔14进入落料管71,再进入水冷器72被降温后进入接料箱73,使用者收集降温后的产物。The product hits the discharge baffle 41 and enters the discharge port 17 along the discharge baffle 41. The product leaves the accommodation chamber 14 and enters the blanking pipe 71, and then enters the water cooler 72 to be cooled and then enters the receiving box 73, where the user collects and cools down. product after.

本发明上述实施例中提供了一种新型的环形反应器,通过置物环31持续转动进行物料传输,可以向进料部件连续投料,加热源加热高效完成反应,出料部件会持续得到产物,实现连续作业,提高工作效率。The above-mentioned embodiment of the present invention provides a new type of annular reactor. The material is transported by the continuous rotation of the storage ring 31, and the material can be continuously fed to the feeding part. The heating source is heated to complete the reaction with high efficiency, and the discharging part will continue to obtain products. Continuous operation, improve work efficiency.

虽然本公开披露如上,但本公开的保护范围并非仅限于此。本领域技术人员在不脱离本公开的精神和范围的前提下,可进行各种变更与修改,这些变更与修改均将落入本发明的保护范围。Although the present disclosure is disclosed above, the scope of protection of the present disclosure is not limited thereto. Those skilled in the art can make various changes and modifications without departing from the spirit and scope of the present disclosure, and these changes and modifications will fall within the protection scope of the present invention.

Claims (15)

1. An annular reactor, characterized by comprising a housing (11), at least one heating source and a rotating member; have in casing (11) and hold chamber (14), the heating source with casing (11) fixed connection, rotating member is including putting thing ring (31) and actuating mechanism, it installs to put thing ring (31) hold in chamber (14), actuating mechanism with it connects to put thing ring (31) drive, be equipped with feed inlet (16) and discharge gate (17) on casing (11), follow put the direction of rotation of thing ring (31), it follows to hold chamber (14) feed inlet (16) extremely regional for the zone of heating between discharge gate (17), the heating source is arranged the zone of heating.
2. The loop reactor of claim 1, wherein the heating zone is in the shape of a sector of a ring, and the central angle of the heating zone is between 0 ° and 360 °.
3. The loop reactor according to claim 2, characterized in that the number of the heating sources is one, and the heating sources are disposed at an upper portion, a lower portion, an outer side or an inner portion of the shell (11).
4. The loop reactor according to claim 2, wherein the number of the heating sources is two or more, a plurality of the heating sources are arranged in the heating zone in an arc shape, and the number of the central angles of the arcs formed between the adjacent heating sources is 15 ° to 60 °.
5. The loop reactor according to any of claims 1 to 4, wherein the heating source is a microwave generator (2), an infrared generator, an electric heater or an electromagnetic induction heater.
6. The loop reactor according to claim 5, characterized in that the microwave generator (2) is a magnetron, a solid state microwave source or a photo-generated microwave source with an emission frequency of 915MHz or 2450 MHz.
7. The loop reactor according to claim 1, characterized in that the drive mechanism comprises a drive motor (32) and a transmission member, the output shaft of the drive motor (32) is connected with the transmission member through the wall surface of the shell (11), and the transmission member is connected with the object ring (31) in a driving manner.
8. An annular reactor according to claim 7, wherein the transmission is a gear (33), a chain (34) or a belt.
9. The loop reactor according to claim 1, characterized in that at least one stirring plate (42) is arranged in the containment chamber (14), the stirring plate (42) being arranged obliquely with respect to the containment ring (31).
10. The loop reactor according to claim 1, characterized in that a distribution plate (43) is arranged in the receiving chamber (14), said distribution plate (43) being arranged at the location of the feed opening (16) for laying material entering the receiving chamber (14) from the feed opening (16) on the object ring (31).
11. The loop reactor according to claim 10, characterized in that a guide is provided in the receiving chamber (14) at the location of the discharge opening (17) for guiding the material on the object ring (31) to the discharge opening (17).
12. The annular reactor according to claim 1, characterized in that an exhaust duct (5) is provided on the top wall (12) of the shell (11), the exhaust duct (5) communicating with the containment chamber (14).
13. The loop reactor according to claim 12, characterized in that the outlet of the exhaust pipe (5) is provided with a flange.
14. The loop reactor according to claim 1, further comprising a feeding member comprising a feed hopper (61) and a screw feeder (62), the feed hopper (61) being connected to an inlet of the screw feeder (62), an outlet of the screw feeder (62) being connected to the feed port (16).
15. The annular reactor according to claim 1, further comprising a discharging part, wherein the discharging part comprises a blanking pipe (71) and a water cooler (72), and two ends of the blanking pipe (71) are respectively connected with the discharging port (17) and the water cooler (72).
CN202010128577.6A 2020-02-28 2020-02-28 Annular reactor Pending CN111359570A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116328677A (en) * 2023-03-30 2023-06-27 江苏正诚锌业科技有限公司 Quality-controllable zinc oxide efficient production device

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006008510A1 (en) * 2004-07-19 2006-01-26 Protensive Limited Spinning disc reactor with shroud or plate for improving gas/liquid contact
CN103333709A (en) * 2013-06-28 2013-10-02 青岛东方循环能源有限公司 Disc-type microwave continuous splitting device and method for splitting waste rubber
CN106190206A (en) * 2016-08-08 2016-12-07 神华集团有限责任公司 Solid heat carrier pyrolysis device

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006008510A1 (en) * 2004-07-19 2006-01-26 Protensive Limited Spinning disc reactor with shroud or plate for improving gas/liquid contact
CN103333709A (en) * 2013-06-28 2013-10-02 青岛东方循环能源有限公司 Disc-type microwave continuous splitting device and method for splitting waste rubber
CN106190206A (en) * 2016-08-08 2016-12-07 神华集团有限责任公司 Solid heat carrier pyrolysis device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116328677A (en) * 2023-03-30 2023-06-27 江苏正诚锌业科技有限公司 Quality-controllable zinc oxide efficient production device

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