技术领域technical field
本实用新型涉及环保领域，特别是涉及一种转轮吸附浓缩RTO废气处理系统。The utility model relates to the field of environmental protection, in particular to a rotary adsorption and concentration RTO waste gas treatment system.
背景技术Background technique
废气净化(Fluegaspurification)主要是指针对工业场所产生的工业废气诸如粉尘颗粒物、烟气烟尘、异味气体、有毒有害气体进行治理的工作。常见的废气净化有工厂烟尘废气净化、车间粉尘废气净化、有机废气净化、废气异味净化、酸碱废气净化、化工废气净化等。RTO(RegenerativeThermalOxidizer)也称作蓄热式氧化炉，用于在高温下将可燃废气氧化成对应的氧化物和水，从而净化废气。然而，目前的废气处理系统净化效果不是很理想。Flue gas purification mainly refers to the treatment of industrial waste gas such as dust particles, flue gas smoke, odor gas, toxic and harmful gas generated in industrial places. Common waste gas purification includes factory smoke and dust waste gas purification, workshop dust waste gas purification, organic waste gas purification, waste gas odor purification, acid-base waste gas purification, chemical waste gas purification, etc. RTO (Regenerative Thermal Oxidizer), also known as regenerative oxidation furnace, is used to oxidize combustible exhaust gas into corresponding oxides and water at high temperature, thereby purifying exhaust gas. However, the purification effect of the current exhaust gas treatment system is not very ideal.
实用新型内容Utility model content
基于此，有必要提供一种处理效果好、污染低的转轮吸附浓缩RTO废气处理系统。Based on this, it is necessary to provide a rotary adsorption concentration RTO waste gas treatment system with good treatment effect and low pollution.
一种转轮吸附浓缩RTO废气处理系统，包括：顺序依次连接的过滤器、多个转轮设备、以及氧化炉，A rotary adsorption and concentration RTO exhaust gas treatment system, including: sequentially connected filters, multiple rotary devices, and an oxidation furnace,
所述过滤器用于初步过滤待处理气体；The filter is used to initially filter the gas to be treated;
所述转轮设备包括转轮箱、设置于所述转轮箱内的转轮体，所述转轮箱具有吸附区及脱附区，所述转轮体位于所述吸附区内，用于净化待处理气体，The runner equipment includes a runner box and a runner body arranged in the runner box, the runner box has an adsorption area and a desorption area, and the runner body is located in the adsorption area for Purify the gas to be treated,
所述吸附区与所述过滤器相连接，以使初步过滤后的待处理气体进入到吸附区内，所述脱附区与所述氧化炉相连接，用于脱附所述转轮体上的挥发性污染物；The adsorption area is connected with the filter so that the pre-filtered gas to be treated enters the adsorption area, and the desorption area is connected with the oxidation furnace for desorbing the gas on the runner body. volatile pollutants;
所述氧化炉用于净化脱附后的挥发性污染物。The oxidation furnace is used to purify the desorbed volatile pollutants.
在其中一个实施例中，所述转轮箱还具有冷却区，用于冷却所述转轮箱内温度。In one of the embodiments, the wheel box also has a cooling zone for cooling the temperature inside the wheel box.
在其中一个实施例中，所述转轮吸附浓缩RTO废气处理系统还包括热交换设备，所述热交换设备与所述氧化炉及所述冷却区相连接。In one of the embodiments, the rotary adsorption concentration RTO waste gas treatment system further includes heat exchange equipment, and the heat exchange equipment is connected with the oxidation furnace and the cooling zone.
在其中一个实施例中，所述氧化炉包括箱体以及设置于所述箱体内的多个蓄热体，所述箱体包括至少两个蓄热室，以及连接并连通所述至少两个蓄热室的连接部。In one of the embodiments, the oxidation furnace includes a box body and a plurality of regenerators arranged in the box body, the box body includes at least two heat storage chambers, and connects and communicates with the at least two heat storage chambers. connection to the heat chamber.
在其中一个实施例中，所述蓄热室为两个。In one of the embodiments, there are two heat storage chambers.
在其中一个实施例中，所述转轮设备为两个，两个所述转轮设备邻近设置，并相连通。In one of the embodiments, there are two turning wheel devices, and the two turning wheel devices are arranged adjacent to each other and communicated with each other.
在其中一个实施例中，还包括若干引风机，所述若干引风机与所述转轮设备、所述氧化炉相连通。In one of the embodiments, several induced draft fans are also included, and the several induced draft fans communicate with the rotary equipment and the oxidation furnace.
在其中一个实施例中，部分所述引风机与所述转轮设备相连通，其余所述引风机与所述氧化炉相连通。In one of the embodiments, some of the induced draft fans are connected with the rotary device, and the rest of the induced draft fans are connected with the oxidation furnace.
在其中一个实施例中，各所述引风机并排设置。In one of the embodiments, the induced draft fans are arranged side by side.
在其中一个实施例中，各所述引风机共用一根引风管。In one of the embodiments, each induced draft fan shares one induced draft pipe.
上述转轮吸附浓缩RTO废气处理系统，由于进行多次净化过程，令待处理气体净化更加彻底，排除后对空气污染更低。此外，热交换设备令转轮吸附浓缩RTO废气处理系统充分利用能源，减少能量的浪费。The above-mentioned rotary adsorption and concentration RTO waste gas treatment system, due to multiple purification processes, makes the gas to be treated more thoroughly purified, and the air pollution is lower after removal. In addition, the heat exchange equipment enables the rotary adsorption and concentration RTO waste gas treatment system to make full use of energy and reduce energy waste.
附图说明Description of drawings
图1为本实用新型一较佳实施例的转轮吸附浓缩RTO废气处理系统的结构示意图；Fig. 1 is the structural representation of the rotary adsorption concentration RTO waste gas treatment system of a preferred embodiment of the present invention;
图2为图1所示转轮吸附浓缩RTO废气处理系统氧化炉的结构示意图；Fig. 2 is the structural representation of the oxidation furnace of the rotary adsorption concentration RTO waste gas treatment system shown in Fig. 1;
图3为图2所示氧化炉不同角度的结构示意图；Fig. 3 is the structural representation of different angles of the oxidation furnace shown in Fig. 2;
图4为图1所示转轮吸附浓缩RTO废气处理系统氧化炉的另一实施例的结构示意图；Fig. 4 is the structural representation of another embodiment of the oxidation furnace of the rotary adsorption concentration RTO waste gas treatment system shown in Fig. 1;
图5为图4所示的氧化炉的局部示意图；Fig. 5 is a partial schematic view of the oxidation furnace shown in Fig. 4;
图6为图1所示转轮吸附浓缩RTO废气处理系统氧化炉的另一实施例的结构示意图；Fig. 6 is the structural representation of another embodiment of the oxidation furnace of the rotary adsorption concentration RTO waste gas treatment system shown in Fig. 1;
图7为图1所示转轮吸附浓缩RTO废气处理系统过滤器的结构示意图；Fig. 7 is a structural schematic diagram of the filter of the rotary adsorption concentration RTO waste gas treatment system shown in Fig. 1;
图8为图1所示转轮吸附浓缩RTO废气处理系统热交换设备的结构示意图。Fig. 8 is a schematic structural view of the heat exchange equipment of the rotary adsorption concentration RTO waste gas treatment system shown in Fig. 1 .
具体实施方式detailed description
为了便于理解本实用新型，下面将参照相关附图对本实用新型进行更全面的描述。附图中给出了本实用新型的较佳实施方式。但是，本实用新型可以以许多不同的形式来实现，并不限于本文所描述的实施方式。相反地，提供这些实施方式的目的是使对本实用新型的公开内容理解的更加透彻全面。In order to facilitate the understanding of the utility model, the utility model will be described more fully below with reference to the relevant drawings. Preferred embodiments of the utility model are provided in the accompanying drawings. However, the invention may be embodied in many different forms and is not limited to the embodiments described herein. On the contrary, the purpose of providing these embodiments is to make the disclosure of the present utility model more thorough and comprehensive.
需要说明的是，当元件被称为“设置于”另一个元件，它可以直接在另一个元件上或者也可以存在居中的元件。当一个元件被认为是“连接”另一个元件，它可以是直接连接到另一个元件或者可能同时存在居中元件。本文所使用的术语“垂直的”、“水平的”、“左”、“右”以及类似的表述只是为了说明的目的，并不表示是唯一的实施方式。It should be noted that when an element is referred to as being “disposed on” another element, it may be directly on the other element or there may also be an intervening element. When an element is referred to as being "connected to" another element, it can be directly connected to the other element or intervening elements may also be present. The terms "vertical," "horizontal," "left," "right," and similar expressions are used herein for purposes of illustration only and are not intended to represent the only embodiments.
除非另有定义，本文所使用的所有的技术和科学术语与属于本实用新型的技术领域的技术人员通常理解的含义相同。本文中在本实用新型的说明书中所使用的术语只是为了描述具体的实施方式的目的，不是旨在于限制本实用新型。本文所使用的术语“及/或”包括一个或多个相关的所列项目的任意的和所有的组合。Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the technical field of this invention. The terminology used herein in the description of the utility model is only for the purpose of describing specific implementations, and is not intended to limit the utility model. As used herein, the term "and/or" includes any and all combinations of one or more of the associated listed items.
如图1所示，其为本实用新型一较佳实施例的转轮吸附浓缩RTO废气处理系统10的结构示意图。As shown in FIG. 1 , it is a schematic structural diagram of a rotary adsorption concentration RTO waste gas treatment system 10 according to a preferred embodiment of the present invention.
转轮吸附浓缩RTO废气处理系统10包括：顺序依次连接的过滤器100、多个转轮设备200、氧化炉300，以及与转轮设备200及氧化炉300连接的热交换设备400。The rotary adsorption concentration RTO exhaust gas treatment system 10 includes: a filter 100 connected in sequence, a plurality of rotary devices 200 , an oxidation furnace 300 , and a heat exchange device 400 connected to the rotary devices 200 and the oxidation furnace 300 .
过滤器100用于对待处理气体初步过滤。例如，顺序设置若干过滤器，待处理气体依次通过各过滤器后进入第一个转轮设备；又如，顺序设置若干转轮设备，待处理气体依次通过各转轮设备后进入氧化炉。The filter 100 is used for preliminary filtering of the gas to be treated. For example, several filters are arranged in sequence, and the gas to be treated enters the first runner device after passing through each filter in turn; another example, several runner devices are arranged in sequence, and the gas to be treated enters the oxidation furnace after passing through each runner device in turn.
转轮设备200包括转轮箱210、设置于转轮箱210内的转轮体220，具体的，转轮箱210具有吸附区211、脱附区212及冷却区213，转轮体220位于吸附区211内，用于净化待处理气体。其中，吸附区211与过滤器100相连接，以使初步过滤后的待处理气体进入到吸附区211内，脱附区212与氧化炉300相连接，用于脱附转轮体220上的挥发性污染物。The wheel equipment 200 includes a wheel box 210 and a wheel body 220 arranged in the wheel box 210. Specifically, the wheel box 210 has an adsorption area 211, a desorption area 212, and a cooling area 213. The wheel body 220 is located in the adsorption area. Zone 211 is used to purify the gas to be treated. Wherein, the adsorption area 211 is connected with the filter 100 so that the pre-filtered gas to be treated enters the adsorption area 211, and the desorption area 212 is connected with the oxidation furnace 300 for the volatilization on the desorption runner body 220. sex pollutants.
氧化炉300用于净化脱附后的挥发性污染物，热交换设备400与冷却区213相连接，用于交换热量。The oxidation furnace 300 is used to purify the desorbed volatile pollutants, and the heat exchange device 400 is connected to the cooling area 213 for exchanging heat.
其他实施例中，热交换设备400也可以省略，此时无需进行热交换。并且转轮设备200中的冷却区213也可以省略。In other embodiments, the heat exchange device 400 may also be omitted, and no heat exchange is required at this time. And the cooling zone 213 in the rotary device 200 can also be omitted.
使用上述转轮吸附浓缩RTO废气处理系统10时，先令待处理气体进入过滤器100，进行初步过滤。初步过滤后，待处理气体进入到一个转轮设备200内的吸附区211内，并通过转轮体220进行第一次净化，大部分的挥发性污染物被转轮体220吸附除去；第一次进化后的待处理气体进入到与之前转轮设备200连接的另一转轮设备200内，进行再次净化；经过多次净化后的待处理气体通过烟囱排出。转轮设备200净化后，对吸附于转轮体220上的挥发性污染物进行脱附，具体的，通过热风处理，令挥发性污染物脱附、并浓缩，之后进入到氧化炉300内。进入到氧化炉300内的气体进行高温氧化分解，以净化挥发性污染物，净化后的挥发性污染物排出转轮吸附浓缩RTO废气处理系统10。转轮设备200脱附挥发性气体后，在冷却区213进行冷却，以使其进入到下一待处理气体净化循环。热交换设备400与冷却区213、氧化炉300相连接，用于交换冷却区213及氧化炉300内排出气体的温度，以为其他设备提供热量。When the above-mentioned rotary adsorption concentration RTO waste gas treatment system 10 is used, the gas to be treated first enters the filter 100 for preliminary filtration. After preliminary filtration, the gas to be treated enters the adsorption area 211 in a runner device 200, and is purified for the first time through the runner body 220, and most of the volatile pollutants are adsorbed and removed by the runner body 220; the first The second-evolved gas to be treated enters another rotary device 200 connected to the previous rotary device 200 for further purification; the gas to be treated after multiple purifications is discharged through the chimney. After the wheel equipment 200 is purified, the volatile pollutants adsorbed on the wheel body 220 are desorbed. Specifically, the volatile pollutants are desorbed and concentrated by hot air treatment, and then enter the oxidation furnace 300 . The gas entering the oxidation furnace 300 is oxidized and decomposed at high temperature to purify volatile pollutants, and the purified volatile pollutants are discharged out of the RTO waste gas treatment system 10 for adsorption and concentration by the runner. After the rotary device 200 desorbs the volatile gas, it is cooled in the cooling zone 213 so that it enters the next purification cycle of the gas to be treated. The heat exchange equipment 400 is connected with the cooling zone 213 and the oxidation furnace 300, and is used for exchanging the temperature of the exhaust gas in the cooling zone 213 and the oxidation furnace 300, so as to provide heat for other equipment.
上述转轮吸附浓缩RTO废气处理系统10，由于进行多次净化过程，令待处理气体净化更加彻底，排除后对空气污染更低。此外，热交换设备400令转轮吸附浓缩RTO废气处理系统10充分利用能源，减少能量的浪费。The above-mentioned rotary adsorption and concentration RTO waste gas treatment system 10, due to multiple purification processes, makes the gas to be treated more thoroughly purified and causes less air pollution after removal. In addition, the heat exchange device 400 enables the rotary adsorption concentration RTO exhaust gas treatment system 10 to fully utilize energy and reduce energy waste.
本实施例中，转轮设备200为两个，两个转轮设备200邻近设置，并相连通。具体的，转轮设备200的转轮厚度为0.3～0.7m，优选为0.4m，进入其内的风速为2～4m/s，优选为2m/s，风阻小于180Pa。需要说明的是，根据实际情况，两个转轮设备200的规格、参数既可以相同，也可以相异。例如，其中一个转轮设备200的转轮体220厚度为0.35m，另一个为0.5m，风速分别为2.5m/s，3m/s。这样，令待处理气体位于不同的环境下进行净化，从而进一步提高净化效果。或者多个轮转设备也可以具有不同厚度的转轮体220，但具有相同的风速及风阻。In this embodiment, there are two wheel devices 200, and the two wheel devices 200 are arranged adjacent to each other and connected. Specifically, the thickness of the runner of the runner device 200 is 0.3-0.7m, preferably 0.4m, the wind speed entering it is 2-4m/s, preferably 2m/s, and the wind resistance is less than 180Pa. It should be noted that, according to the actual situation, the specifications and parameters of the two runner devices 200 may be the same or different. For example, the thickness of the runner body 220 of one of the runner devices 200 is 0.35m, and that of the other is 0.5m, and the wind speeds are 2.5m/s and 3m/s respectively. In this way, the gas to be treated is purified in different environments, thereby further improving the purification effect. Alternatively, multiple rotating devices may have different thicknesses of the runner body 220, but have the same wind speed and wind resistance.
此外，需要说明的是，当转轮设备200为多个时，多个转轮设备200可同时进行不同的处理步骤。例如，当转轮设备200为四个时，其中的两个转轮设备200用于净化气体，进行吸附，另外两个转轮设备200脱附转轮体220上的挥发性污染物，此时，多个转轮设备200之间设有阀门，用于控制彼此连通或断开。或者，多个设备之间也可以通过转换管连接，用于切换连接不同的设备。这样，转轮吸附浓缩RTO废气处理系统10可持续净化废气，提高了其处理能力。In addition, it should be noted that when there are multiple wheel devices 200 , the multiple wheel devices 200 can simultaneously perform different processing steps. For example, when there are four runner devices 200, two of the runner devices 200 are used to purify the gas for adsorption, and the other two runner devices 200 desorb the volatile pollutants on the runner body 220. , valves are provided between the plurality of wheel devices 200 for controlling communication or disconnection with each other. Alternatively, multiple devices can also be connected through a conversion tube for switching and connecting different devices. In this way, the rotary adsorption and concentration RTO waste gas treatment system 10 can continuously purify waste gas and improve its treatment capacity.
本实施例中，转轮吸附浓缩RTO废气处理系统10还包括若干引风机500，若干引风机500与转轮设备200、氧化炉300相连通，用于引导气体流动。具体的，转轮吸附浓缩RTO废气处理系统10中每一设备附近均设有一引风机500。并且，转轮吸附浓缩RTO废气处理系统内的各设备通过多个管道相连接，管道上设有压力表及温度表，用于监控转轮吸附浓缩RTO废气处理系统10内的温度及压强。例如，每个管道上均设有压力表及温度表。此外，多个管道上均设有控制阀。例如，转轮吸附浓缩RTO废气处理系统内的过滤器、多个转轮设备、氧化炉，分别通过多个管道相连接。其他实施例中，也可以部分引风机与转轮设备相连通，其余引风机与氧化炉相连通。例如，各引风机并排设置。或者，各引风机共用一根引风管。In this embodiment, the rotary adsorption concentration RTO waste gas treatment system 10 also includes several induced draft fans 500, which are connected with the rotary device 200 and the oxidation furnace 300 for guiding the gas flow. Specifically, an induced draft fan 500 is provided near each device in the rotary adsorption concentration RTO waste gas treatment system 10 . Moreover, each device in the rotor adsorption concentration RTO exhaust gas treatment system is connected through multiple pipelines, and the pipelines are provided with pressure gauges and temperature gauges for monitoring the temperature and pressure in the rotor adsorption concentration RTO exhaust gas treatment system 10 . For example, each pipeline is provided with a pressure gauge and a temperature gauge. In addition, control valves are provided on multiple pipelines. For example, the filters in the rotary adsorption concentration RTO waste gas treatment system, multiple rotary devices, and oxidation furnaces are connected through multiple pipelines. In other embodiments, part of the induced draft fans may also be connected with the runner equipment, and the rest of the induced draft fans may be connected with the oxidation furnace. For example, the induced draft fans are arranged side by side. Alternatively, each induced draft fan shares one induced air pipe.
请一并参阅图2及图3，其分别为图1所示转轮吸附浓缩RTO废气处理系统10的氧化炉300的结构示意图，及其不同角度的结构示意图。Please refer to FIG. 2 and FIG. 3 together, which are schematic structural diagrams of the oxidation furnace 300 of the rotary adsorption concentration RTO waste gas treatment system 10 shown in FIG. 1 , and structural schematic diagrams from different angles.
氧化炉300包括箱体310以及设置于箱体310内的多个蓄热体320。其中，箱体310包括至少两个蓄热室311，以及连接并连通至少两个蓄热室311的连接部312。具体的，蓄热室311的侧壁上开设有进风口311A及出风口311B，进风口311A及出风口311B均位于侧壁邻近底壁的区域，蓄热室311及/或连接部312上开设有与蓄热室311相连通的加热孔，用于通过其对箱体310内的空气加热。多个蓄热体320间隔设置于箱体310的内表面上，用于蓄热。The oxidation furnace 300 includes a box body 310 and a plurality of thermal accumulators 320 installed in the box body 310 . Wherein, the box body 310 includes at least two heat storage chambers 311 , and a connecting portion 312 connecting and communicating with the at least two heat storage chambers 311 . Specifically, an air inlet 311A and an air outlet 311B are provided on the side wall of the regenerator 311, and both the air inlet 311A and the air outlet 311B are located in the area adjacent to the bottom wall of the side wall. There is a heating hole communicating with the heat storage chamber 311 for heating the air in the box body 310 through it. A plurality of heat accumulators 320 are arranged at intervals on the inner surface of the box body 310 for heat storage.
本实施例中，蓄热室311为三个，三个蓄热室311及连接部312围成一M形箱体310，其中连接部312位于蓄热室311远离放置面的一端。其他实施例中，蓄热室311也可以为多个，多个蓄热室311均与连接部312相连接，例如多个蓄热室311均位于连接部312的一侧，且多个蓄热室311并列间隔设置。又或者，蓄热室311为两个，两个蓄热室311与连接部312围成M形箱体310。In this embodiment, there are three regenerators 311 , and the three regenerators 311 and the connection part 312 enclose an M-shaped box 310 , wherein the connection part 312 is located at the end of the regenerator 311 away from the placement surface. In other embodiments, there may be multiple heat storage chambers 311, and the multiple heat storage chambers 311 are all connected to the connection part 312, for example, the multiple heat storage chambers 311 are located on one side of the connection part 312, and the multiple heat storage chambers The chambers 311 are arranged side by side at intervals. Alternatively, there are two regenerators 311 , and the two regenerators 311 and the connecting portion 312 enclose an M-shaped box 310 .
使用上述氧化炉300时，先令待处理气体由其中一蓄热室311上的进风口311A进入到箱体310内，以使待处理气体经由连接部312传递到另一蓄热室311内。通过加热孔对箱体310内的待处理气体进行加热，令其氧化分解。加热后，温度较高的待处理气体及处理后的气体穿过多个蓄热体320，并将热量传递到蓄热体320上。待处理气体分解后，经由多个蓄热体320传递到另一蓄热室311的出风口311B，并排出。当蓄热体320的温度达到能够氧化分解待处理气体时，关闭加热孔，令待处理气体经由其中一个进风口311A进入到箱体310内，进入到箱体310内的待处理气体通过多个蓄热体320加热后，氧化分解，并从另一个出风口排出。When using the above-mentioned oxidation furnace 300 , the gas to be treated first enters the box body 310 through the air inlet 311A on one of the regenerators 311 , so that the gas to be treated is transferred to the other regenerator 311 through the connecting portion 312 . The gas to be treated in the box 310 is heated through the heating holes to oxidize and decompose it. After heating, the high temperature gas to be treated and the treated gas pass through multiple heat storage bodies 320 and transfer heat to the heat storage bodies 320 . After the gas to be treated is decomposed, it is delivered to the air outlet 311B of another heat storage chamber 311 through a plurality of heat storage bodies 320 and discharged. When the temperature of the regenerator 320 reaches the temperature that can oxidize and decompose the gas to be treated, the heating hole is closed, so that the gas to be treated enters the box body 310 through one of the air inlets 311A, and the gas to be treated that enters the box body 310 passes through multiple After the thermal storage body 320 is heated, it oxidizes and decomposes, and is discharged from another air outlet.
上述氧化炉300，由于具有多个蓄热室311，令待处理气体能够充分氧化分解，进而提高氧化炉300的处理效率及处理效果。由于出风口311B及进风口311A均设置于蓄热室311的侧壁上，相比传统设置于底壁上，减少了箱体310的高度，从而方便放置，并且还降低了设备阻力，令气体更流畅。此外，多个蓄热体320能够储存足够热量以分解待处理气体，从而节约了能源，无需时刻通过加热孔进行加热。The above-mentioned oxidation furnace 300 has a plurality of regenerators 311 , so that the gas to be treated can be fully oxidized and decomposed, thereby improving the treatment efficiency and treatment effect of the oxidation furnace 300 . Since the air outlet 311B and the air inlet 311A are both arranged on the side wall of the regenerator 311, compared with the traditional arrangement on the bottom wall, the height of the box body 310 is reduced, which is convenient for placement, and also reduces the resistance of the equipment, making the gas more fluid. In addition, the plurality of heat accumulators 320 can store enough heat to decompose the gas to be treated, thereby saving energy, and there is no need to heat through the heating holes all the time.
本实施例中，每个蓄热室311的侧壁上均开设有进风口311A及出风口311B。并且，进风口311A及出风口311B位于蓄热室311相异的表面上。这样，当待处理气体通过其中一个蓄热室311的进风口311A进入时，由另一个出风口311B排出，令待处理气体反应充分，并且能够将更多地热量交换到蓄热体320上。In this embodiment, an air inlet 311A and an air outlet 311B are opened on the side wall of each regenerator 311 . Moreover, the air inlet 311A and the air outlet 311B are located on different surfaces of the heat storage chamber 311 . In this way, when the gas to be treated enters through the air inlet 311A of one of the heat storage chambers 311 , it is discharged from the other air outlet 311B, so that the gas to be treated can fully react and exchange more heat to the heat storage body 320 .
为了方便实用，蓄热室311的侧壁上还设置有至少一观察区域311C，用于观察蓄热室311内的情况。具体的，观察区域311C邻近蓄热室311的底壁设置，且与进风口311A、出风口311B分别位于蓄热室311不同的表面上。例如，所述观察区域311C为矩形观察区域。For convenience and practicality, at least one observation area 311C is provided on the side wall of the heat storage chamber 311 for observing the situation in the heat storage chamber 311 . Specifically, the observation area 311C is set adjacent to the bottom wall of the heat storage chamber 311 , and is located on a different surface of the heat storage chamber 311 than the air inlet 311A and the air outlet 311B. For example, the observation area 311C is a rectangular observation area.
本实施例中，加热孔设置于连接部312的中部。其他实施例中，加热孔也可以设置于蓄热室311上；或者加热孔也可以为多个，多个加热孔同时设置于蓄热室311及连接部312上。In this embodiment, the heating hole is disposed in the middle of the connecting portion 312 . In other embodiments, the heating holes may also be arranged on the regenerator 311 ; or there may be multiple heating holes, and the plurality of heating holes are arranged on the regenerator 311 and the connecting portion 312 at the same time.
根据实际需要，氧化炉300还包括缓冲箱330，缓冲箱330与出风口311B相连接并连通，以使分解后的气体经由缓冲箱330排出。具体的，缓冲箱330具有缓冲出风口及缓冲进风口，缓冲进风口与出风口相连通，以使分解后的气体，经由出风口311B、缓冲进风口、缓冲出风口排出。其中，缓冲出风口与出风口311B所在平面垂直，并且缓冲出风口位于缓冲箱330的顶端。这样，令气体更加流畅。又如，出风口311B的面积小于缓冲进风口的面积，缓冲进风口的面积小于缓冲出风口的面积，这样，有利于使分解后的气体降速排出。According to actual needs, the oxidation furnace 300 further includes a buffer box 330 , which is connected and communicated with the air outlet 311B, so that the decomposed gas is discharged through the buffer box 330 . Specifically, the buffer box 330 has a buffer air outlet and a buffer air inlet, and the buffer air inlet is connected to the air outlet, so that the decomposed gas is discharged through the air outlet 311B, the buffer air inlet, and the buffer air outlet. Wherein, the buffer air outlet is perpendicular to the plane where the air outlet 311B is located, and the buffer air outlet is located at the top of the buffer box 330 . In this way, the gas flows more smoothly. For another example, the area of the air outlet 311B is smaller than the area of the buffer air inlet, and the area of the buffer air inlet is smaller than the area of the buffer air outlet, which is conducive to reducing the decomposed gas and discharging it.
需要指出的是，缓冲箱330可拆卸地设置于箱体310上。例如缓冲箱330与箱体310卡接、插接、螺接等。例如，还设置有安装套，缓冲箱330固定设置于安装套上，安装套套置于箱体310的套接位处，这样易于安装和拆卸缓冲箱330，使用非常方便。It should be noted that the buffer box 330 is detachably disposed on the box body 310 . For example, the buffer box 330 and the box body 310 are clamped, plugged, screwed, and the like. For example, a mounting sleeve is also provided, and the buffer box 330 is fixedly arranged on the mounting sleeve, and the mounting sleeve is placed at the socket position of the box body 310, so that the buffer box 330 is easy to install and disassemble, and is very convenient to use.
本实施例中，多个蓄热体320层叠间隔设置。并且，蓄热室311及连接部312内均设有蓄热体320，其中，蓄热体320的周缘与箱体310内壁相连接。其他实施例中，蓄热体320也可以仅设置于蓄热室311内，或者仅设置于连接部312内。In this embodiment, a plurality of thermal accumulators 320 are stacked and arranged at intervals. Moreover, a heat storage body 320 is disposed inside the heat storage chamber 311 and the connecting portion 312 , wherein the periphery of the heat storage body 320 is connected to the inner wall of the box body 310 . In other embodiments, the heat storage body 320 may also be only disposed in the heat storage chamber 311 , or only disposed in the connecting portion 312 .
请一并参阅图4，其为图1所示转轮吸附浓缩RTO废气处理系统10另一实施例氧化炉301的结构示意图。Please also refer to FIG. 4 , which is a schematic structural diagram of an oxidation furnace 301 of another embodiment of the rotary adsorption concentration RTO waste gas treatment system 10 shown in FIG. 1 .
氧化炉301包括：包括箱体310、设置于箱体310内的多个蓄热体320，以及设置于蓄热体320上的滤气层340。其中，箱体310包括至少两个蓄热室311，以及连接并连通至少两个蓄热室311的连接部312，蓄热室311开设有进风口311A及出风口311B，蓄热室311及/或连接部312上开设有与蓄热室311相连通的加热孔，即加热孔既可以单独开设于蓄热室311或者连接部312上，也可以同时开设于蓄热室311及连接部312上；多个蓄热体320间隔设置于箱体310的内表面上；滤气层340层叠设置于蓄热体320上，并遮盖蓄热体320，滤气层340用于过滤通过蓄热体320的气体。The oxidation furnace 301 includes: a box body 310 , a plurality of regenerators 320 arranged in the box body 310 , and a gas filter layer 340 arranged on the regenerators 320 . Wherein, the box body 310 includes at least two heat storage chambers 311, and a connecting portion 312 connecting and communicating with at least two heat storage chambers 311. The heat storage chamber 311 is provided with an air inlet 311A and an air outlet 311B. The heat storage chambers 311 and/or Or the connection part 312 is provided with a heating hole that communicates with the regenerator 311, that is, the heating hole can be opened separately on the regenerator 311 or the connection part 312, or can be opened on the regenerator 311 and the connection part 312 at the same time A plurality of regenerators 320 are arranged at intervals on the inner surface of the box body 310; the air filter layer 340 is stacked on the regenerator 320 and covers the regenerator 320, and the air filter layer 340 is used for filtering through the regenerator 320 gas.
使用上述氧化炉301时，先令待处理气体由其中一蓄热室311上的进风口311A进入到箱体310内，以使待处理气体经由连接部312传递到另一蓄热室311内。通过加热孔对箱体310内的待处理气体进行加热，令其氧化分解。加热后，温度较高的待处理气体及处理后的气体穿过多个蓄热体320，并将热量传递到蓄热体320上，具体的，气体先通过与蓄热体320连接的滤气层340，进行过滤，之后再通过蓄热体320。待处理气体分解后，经由多个蓄热体320传递到另一蓄热室311的出风口311B，并排出。当蓄热体320的温度达到能够氧化分解待处理气体时，关闭加热孔，令待处理气体经由其中一个进风口311A进入到箱体310内，进入到箱体310内的待处理气体通过多个蓄热体320加热后，氧化分解，并从另一个出风口排出。When using the above-mentioned oxidation furnace 301 , the gas to be treated first enters the box body 310 from the air inlet 311A on one of the regenerators 311 , so that the gas to be treated is transferred to the other regenerator 311 through the connecting portion 312 . The gas to be treated in the box 310 is heated through the heating holes to oxidize and decompose it. After heating, the higher-temperature gas to be treated and the treated gas pass through a plurality of regenerators 320, and transfer heat to the regenerators 320. Specifically, the gas first passes through the filter gas connected to the regenerators 320. Layer 340 for filtration before passing through heat storage body 320 . After the gas to be treated is decomposed, it is delivered to the air outlet 311B of another heat storage chamber 311 through a plurality of heat storage bodies 320 and discharged. When the temperature of the regenerator 320 reaches the temperature that can oxidize and decompose the gas to be treated, the heating hole is closed, so that the gas to be treated enters the box body 310 through one of the air inlets 311A, and the gas to be treated that enters the box body 310 passes through multiple After the thermal storage body 320 is heated, it oxidizes and decomposes, and is discharged from another air outlet.
上述氧化炉301，滤气层340能够滤去待处理气体中的微小颗粒，令蓄热体320不易堵塞，进而保证了箱体310内气体流动的流畅性，并且能够辅助处理气体，提高氧化炉301的处理效果。此外，多个蓄热体320能够储存足够热量以分解待处理气体，从而节约了能源，无需时刻通过加热孔进行加热。The above-mentioned oxidation furnace 301, the gas filter layer 340 can filter out the tiny particles in the gas to be treated, so that the regenerator 320 is not easy to block, thereby ensuring the smoothness of the gas flow in the box 310, and can assist in the treatment of gas, improving the efficiency of the oxidation furnace. 301 processing effect. In addition, the plurality of heat accumulators 320 can store enough heat to decompose the gas to be treated, thereby saving energy, and there is no need to heat through the heating holes all the time.
请一并参阅图5，其为图4所示氧化炉301的局部示意图。Please also refer to FIG. 5 , which is a partial schematic diagram of the oxidation furnace 301 shown in FIG. 4 .
本实施例中，蓄热体320包括炉栅321以及设置于炉栅321上的本体322，其中，炉栅321设置于箱体310的内壁上，滤气层340设置于炉栅321上，并与本体322分别位于炉栅321的两侧。In this embodiment, the regenerator 320 includes a grate 321 and a body 322 disposed on the grate 321, wherein the grate 321 is disposed on the inner wall of the box body 310, the gas filter layer 340 is disposed on the grate 321, and The body 322 and the body 322 are respectively located on two sides of the grate 321 .
其他实施例中，每个蓄热体320上也可以设置多个滤气层340，例如，每个蓄热体320上设有两个滤气层340，且分别位于炉栅321的两侧，即炉栅位于两个滤气层之间。又如，炉栅321的一侧设有多个层叠设置的滤气层340，多个滤气层340的材质相异，用于滤去不同的杂质及废气。这样，令滤气层340的过滤效果更佳。In other embodiments, multiple air filter layers 340 may also be provided on each regenerator 320, for example, each regenerator 320 is provided with two air filter layers 340, which are respectively located on both sides of the grate 321, That is, the grate is located between the two air filter layers. As another example, one side of the grate 321 is provided with a plurality of stacked gas filter layers 340 , and the materials of the multiple gas filter layers 340 are different, and are used to filter out different impurities and waste gas. In this way, the filtering effect of the air filter layer 340 is better.
本实施例中，滤气层340可拆卸地设置于蓄热体320上。具体的，炉栅321上设有挂钩323，滤气层340包括挂盘341以及设置于挂盘341内的滤气主体，挂盘341与挂钩323挂接，以使滤气层340与挂钩323挂接。其中，挂钩323为多个，多个挂钩323均匀分布于炉栅321上。In this embodiment, the air filter layer 340 is detachably disposed on the heat storage body 320 . Specifically, a hook 323 is provided on the grate 321, and the air filter layer 340 includes a hanging plate 341 and a filter air body arranged in the hanging plate 341. The hanging plate 341 is hooked with the hook 323, so that the air filter layer 340 and the hook 323 mount. Wherein, there are multiple hooks 323 , and the multiple hooks 323 are evenly distributed on the grate 321 .
进一步的，挂钩323包括彼此连接的第一连接体323A及第二连接体323B，其中，第一连接体323A设置于炉栅321上，第二连接体323B卡接挂盘341，具体的，挂盘341上开设有挂接孔，第二连接体323B穿设挂接孔，并与挂盘341开设挂接孔的区域卡接。挂钩323呈L形，并且第一连接体323A与第二连接体323B的连接区域具有圆角，以增强挂钩323的强度，避免断裂。根据实际情况，第一连接体323A与第二连接体323B之间可形成直角，或者锐角，例如30～80度，优选为70度。这样，不仅令挂钩连接更加稳定，并且不宜断裂。Further, the hook 323 includes a first connecting body 323A and a second connecting body 323B connected to each other, wherein the first connecting body 323A is arranged on the grate 321, and the second connecting body 323B is clamped to the hanging plate 341, specifically, the hanging A hooking hole is opened on the tray 341 , and the second connecting body 323B is pierced with the hooking hole, and engages with the area of the hanging tray 341 where the hooking hole is opened. The hook 323 is L-shaped, and the connection area between the first connecting body 323A and the second connecting body 323B has rounded corners, so as to enhance the strength of the hook 323 and avoid breakage. According to actual conditions, a right angle or an acute angle may be formed between the first connecting body 323A and the second connecting body 323B, for example, 30-80 degrees, preferably 70 degrees. In this way, not only the hook connection is more stable, but also not easy to break.
需要指出的是，根据实际情况，炉栅321可拆卸地设置于箱体310内壁上。例如，炉栅321与箱体310卡接、螺接、插接等。例如，还设置有插接套，炉栅321固定设置于插接套上，插接套插置于箱体310内壁上的插接位处，这样易于安装和拆卸炉栅321，使用非常方便。It should be pointed out that, according to the actual situation, the grate 321 is detachably arranged on the inner wall of the box body 310 . For example, the grate 321 is clamped, screwed, inserted, etc. with the box body 310 . For example, a socket sleeve is also provided, and the grate 321 is fixedly arranged on the socket sleeve, and the socket sleeve is inserted at the socket position on the inner wall of the box body 310, so that it is easy to install and disassemble the grate 321, and it is very convenient to use.
请一并参阅图6，其为图1所示转轮吸附浓缩RTO废气处理系统10氧化炉302的另一实施例的结构示意图。Please also refer to FIG. 6 , which is a schematic structural diagram of another embodiment of the oxidation furnace 302 of the rotary adsorption concentration RTO waste gas treatment system 10 shown in FIG. 1 .
氧化炉302包括箱体310、设置于箱体310内的多个蓄热体320，以及设置于箱体310上的防爆装置350。其中，箱体310包括至少两个蓄热室311，以及连接并连通至少两个蓄热室311的连接部312，蓄热室311的侧壁上开设有进风口311A及出风口311B，蓄热室311及/或连接部312上开设有与蓄热室311相连通的加热孔；多个蓄热体320间隔设置于箱体310的内表面上；防爆装置350包括均设置于箱体310上的防爆门以及报警部，防爆门活动设置于箱体310上，以触发报警部。The oxidation furnace 302 includes a box body 310 , a plurality of regenerators 320 arranged in the box body 310 , and an explosion-proof device 350 arranged on the box body 310 . Wherein, the box body 310 includes at least two heat storage chambers 311, and a connecting portion 312 connecting and communicating with the at least two heat storage chambers 311. The side walls of the heat storage chambers 311 are provided with an air inlet 311A and an air outlet 311B to store heat. The chamber 311 and/or the connecting portion 312 are provided with heating holes communicating with the regenerator 311; a plurality of regenerators 320 are arranged at intervals on the inner surface of the box body 310; The explosion-proof door and the alarm part, the explosion-proof door is set on the box body 310 to trigger the alarm part.
使用上述氧化炉302时，先令待处理气体由其中一蓄热室上的进风口311A进入到箱体310内，以使待处理气体经由连接部312传递到另一蓄热室内。通过加热孔对箱体310内的待处理气体进行加热，令其氧化分解。加热后，温度较高的待处理气体及处理后的气体穿过多个蓄热体320，并将热量传递到蓄热体320上。待处理气体分解后，经由多个蓄热体320传递到另一蓄热室的出风口311B，并排出。当蓄热体320的温度达到能够氧化分解待处理气体时，关闭加热孔，令待处理气体经由其中一个进风口311A进入到箱体310内，进入到箱体310内的待处理气体通过多个蓄热体320加热后，氧化分解，并从另一个出风口排出。当箱体310内的温度过高，进而造成压力过高时，防爆门被高压气体推动，以使其远离箱体310运动，当运动到预警位置时，防爆门触发报警部，报警部报警，以警示使用者。When using the above-mentioned oxidation furnace 302 , the gas to be treated is firstly allowed to enter the box body 310 through the air inlet 311A on one of the regenerators, so that the gas to be treated is transferred to the other regenerator through the connecting portion 312 . The gas to be treated in the box 310 is heated through the heating holes to oxidize and decompose it. After heating, the high temperature gas to be treated and the treated gas pass through multiple heat storage bodies 320 and transfer heat to the heat storage bodies 320 . After the gas to be treated is decomposed, it is delivered to the air outlet 311B of another heat storage chamber via a plurality of heat storage bodies 320 and discharged. When the temperature of the regenerator 320 reaches the temperature that can oxidize and decompose the gas to be treated, the heating hole is closed, so that the gas to be treated enters the box body 310 through one of the air inlets 311A, and the gas to be treated that enters the box body 310 passes through multiple After the thermal storage body 320 is heated, it oxidizes and decomposes, and is discharged from another air outlet. When the temperature inside the box 310 is too high and the pressure is too high, the explosion-proof door is pushed by the high-pressure gas so that it moves away from the box 310. When it moves to the warning position, the explosion-proof door triggers the alarm unit, and the alarm unit gives an alarm. to warn users.
上述氧化炉302，由于具有多个蓄热室311，令待处理气体能够充分氧化分解，进而提高氧化炉302的处理效率及处理效果。多个蓄热体320能够储存足够热量以分解待处理气体，从而节约了能源，无需时刻通过加热孔进行加热。此外，报警装置能够提前预警，避免氧化炉302爆炸，提高了安全性能。The oxidation furnace 302 has a plurality of regenerators 311 , so that the gas to be treated can be fully oxidized and decomposed, thereby improving the treatment efficiency and treatment effect of the oxidation furnace 302 . The plurality of heat accumulators 320 can store enough heat to decompose the gas to be treated, thereby saving energy, and there is no need to heat through the heating holes all the time. In addition, the alarm device can give an early warning to prevent the oxidation furnace 302 from exploding, thereby improving safety performance.
报警部包括设置于箱体310上的报警主体，以及与报警主体电连接的限位开关。其中，限位开关用于当防爆门远离箱体310并到达限位开关的位置时被触发，也可以理解为，当箱内压力过大时，防爆门远离箱体310运动，当防爆门触碰到限位开关后，触发限位开关，进而开启报警主体。The alarm part includes an alarm body arranged on the box body 310, and a limit switch electrically connected to the alarm body. Wherein, the limit switch is used to be triggered when the explosion-proof door is away from the box body 310 and reaches the position of the limit switch. After touching the limit switch, trigger the limit switch, and then turn on the alarm main body.
根据是需要，本实施例中，报警部还包括与限位开关相连接的指示灯，指示灯位于蓄热室311上，用于指示限位开关是否被触发，例如，指示灯位于蓄热室311的进风口311A区域。其他实施例中，报警部还包括与限位开关相连接的蜂鸣器，蜂鸣器位于箱体310上，当限位开关被触发后，用于发出警报声，以警示使用者。According to needs, in this embodiment, the alarm part also includes an indicator light connected to the limit switch. The indicator light is located on the regenerator 311 to indicate whether the limit switch is triggered. For example, the indicator light is located in the regenerator. The air inlet 311A area of 311. In other embodiments, the alarm part further includes a buzzer connected to the limit switch. The buzzer is located on the box body 310 and is used to send out an alarm sound to warn users when the limit switch is triggered.
本实施例中，防爆门位于连接部312上，并位于连接部312的顶端。其他实施例中，防爆门也可以位于其他位置。例如，防爆门位于蓄热室311上。又如，防爆门为多个，多个防爆门设置于箱体310的不同区域上，具体的，连接部312及蓄热室311上均设有防爆门。In this embodiment, the explosion-proof door is located on the connecting portion 312 and at the top of the connecting portion 312 . In other embodiments, the explosion-proof door can also be located at other positions. For example, an explosion vent is located on the regenerator 311 . In another example, there are multiple explosion-proof doors, and the multiple explosion-proof doors are arranged on different areas of the box body 310 . Specifically, explosion-proof doors are provided on the connecting portion 312 and the regenerator 311 .
箱体310开设防爆口，防爆门与防爆口扣合，封闭防爆口，并与箱体310内相连通。根据需要，防爆门上设有连接链，连接链连接防爆门与箱体310，以避免防爆门喷出后遗失。The box body 310 is provided with an explosion-proof opening, and the explosion-proof door is fastened with the explosion-proof opening to close the explosion-proof opening and communicate with the inside of the box body 310 . According to needs, a connection chain is provided on the explosion-proof door, and the connection chain connects the explosion-proof door and the box body 310, so as to prevent the explosion-proof door from being lost after spraying out.
需要指出的是，防爆口的周缘还设有缓冲垫，防爆门与缓冲垫相抵接，用于减少防爆门来回碰撞箱体310的噪音。本实施例中，防爆门覆盖部分缓冲垫，这样，令缓冲性能更佳。It should be pointed out that a buffer pad is provided around the explosion-proof opening, and the explosion-proof door is in contact with the buffer pad to reduce the noise of the explosion-proof door colliding with the box 310 back and forth. In this embodiment, the explosion-proof door covers part of the buffer pad, so that the buffer performance is better.
请一并参阅图7，其为图1所示转轮吸附浓缩RTO废气处理系统10过滤器100的结构示意图。Please also refer to FIG. 7 , which is a schematic structural diagram of the filter 100 of the rotary adsorption concentration RTO waste gas treatment system 10 shown in FIG. 1 .
过滤器100包括壳体110、设置于壳体110内的连接装置120，以及设置于连接装置120上的多个过滤层130。具体的，壳体110开设有过滤进风口111及过滤出风口112，过滤出风口112与进风口311A相连接，以使过滤后的气体经由进风口311A进入到氧化炉300内。连接装置120与壳体110围成通风道，且通风道与过滤出风口112、进风口311A相连通；多个过滤层130层叠间隔设置于通风道内，且过滤层130与通风方向形成夹角。也可以理解为，过滤层130与通风方向非平行设置。The filter 100 includes a housing 110 , a connection device 120 disposed in the housing 110 , and a plurality of filter layers 130 disposed on the connection device 120 . Specifically, the casing 110 is provided with a filter air inlet 111 and a filter air outlet 112, and the filter air outlet 112 is connected with the air inlet 311A, so that the filtered gas enters the oxidation furnace 300 through the air inlet 311A. The connection device 120 and the housing 110 enclose an air duct, and the air duct communicates with the filter air outlet 112 and the air inlet 311A; multiple filter layers 130 are stacked and arranged in the air duct at intervals, and the filter layers 130 form an included angle with the ventilation direction. It can also be understood that the filter layer 130 is arranged non-parallel to the ventilation direction.
其他实施例中，又如，多个过滤层130层叠间隔设置于通风道内，且相邻过滤层130之间设置有若干挡风槽，其凸置于通风道内的壳体110上，用于减缓风速且形成朝向过滤层130中部位置的风向，令待处理气体过滤更加彻底；例如，挡风槽具有楔形截面。又如，过滤层130的边缘处增厚设置。In other embodiments, as another example, a plurality of filter layers 130 are stacked and spaced in the air duct, and a number of wind-shielding grooves are arranged between adjacent filter layers 130, which are protruded on the housing 110 in the air duct for slowing down. The wind speed and the wind direction towards the middle of the filter layer 130 make the gas to be treated be filtered more thoroughly; for example, the wind-shielding slot has a wedge-shaped cross-section. As another example, the edge of the filter layer 130 is thickened.
需要说明的时，过滤器100也可以位于氧化炉300与轮转设备之间，以过滤气体。When it needs to be explained, the filter 100 may also be located between the oxidation furnace 300 and the rotary equipment to filter the gas.
上述氧化炉300由于过滤器100对待处理气体进行初步过滤，滤去其中易凝结的微粒物质及粉尘，继而减小待处理气体对氧化炉300、轮转设备内通风效果的影响，令其通风更顺畅，进而减小安全隐患。由于多个过滤层130层叠设置，一方面令待处理气体的过滤效果更佳，提高净化效率，另一方面减小了过滤器100的占地面积。The above-mentioned oxidation furnace 300 preliminarily filters the gas to be treated by the filter 100 to filter out the easily condensed particulate matter and dust, thereby reducing the influence of the gas to be treated on the ventilation effect of the oxidation furnace 300 and the rotary equipment, making its ventilation smoother , thereby reducing potential safety hazards. Since a plurality of filter layers 130 are stacked, on the one hand, the filtering effect of the gas to be treated is improved, and the purification efficiency is improved; on the other hand, the occupied area of the filter 100 is reduced.
本实施例中，连接装置120包括连接隔板121、第一连接件122及第二连接件123。其中，第一连接件122设置于隔板上，第二连接件123设置于壳体110上，并与隔板相对设置。具体的，第二连接件123设置于围成通风道的壳体110内壁上，每一第二连接件123均与一第一连接件122对应，并且每个过滤层130的两端均分别与相对应的第一连接件122及第二连接件123相连接，以固定过滤层130。这样，令过滤层130更稳定地设置于壳体110内。In this embodiment, the connecting device 120 includes a connecting partition 121 , a first connecting part 122 and a second connecting part 123 . Wherein, the first connecting part 122 is disposed on the partition, and the second connecting part 123 is disposed on the casing 110 and is opposite to the partition. Specifically, the second connectors 123 are arranged on the inner wall of the housing 110 that encloses the air duct, each second connector 123 corresponds to a first connector 122, and both ends of each filter layer 130 are respectively connected to The corresponding first connecting part 122 and the second connecting part 123 are connected to fix the filter layer 130 . In this way, the filter layer 130 is more stably disposed in the casing 110 .
需要指出的是，其他实施例中，也可以省略第二连接件123，此时，过滤层130仅设置于第二连接件123上。It should be noted that, in other embodiments, the second connecting member 123 may also be omitted, and at this time, the filter layer 130 is only disposed on the second connecting member 123 .
根据实际情况，过滤层130可拆卸地设置于第一连接件122及第二连接件123上，具体的，过滤层130卡接于第一连接件122及第二连接件123上。这样方便更换过滤层130、清洗及维修过滤器100。需要指出的是，过滤层130也可以固定连接于第一连接件122及第二连接件123上。According to the actual situation, the filter layer 130 is detachably disposed on the first connector 122 and the second connector 123 , specifically, the filter layer 130 is clamped on the first connector 122 and the second connector 123 . In this way, it is convenient to replace the filter layer 130 , clean and maintain the filter 100 . It should be pointed out that the filter layer 130 can also be fixedly connected to the first connecting part 122 and the second connecting part 123 .
本实施例中，隔板将壳体110分隔成缓冲区域101及通风区域102，其中，通风道、进风口311A位于通风区域102内，出风口311B位于缓冲区域101内。也可以理解为，隔板，部分壳体110侧壁围成通风道，即通风区域102与通风道重合。In this embodiment, the partition divides the housing 110 into a buffer area 101 and a ventilation area 102 , wherein the ventilation channel and the air inlet 311A are located in the ventilation area 102 , and the air outlet 311B is located in the buffer area 101 . It can also be understood that the partition board and part of the side walls of the casing 110 enclose an air passage, that is, the ventilation area 102 coincides with the air passage.
待处理气体通过通风道后，进入到缓冲区域101中，缓冲区域101减缓气体的流速，从而令其更平缓的进入到氧化炉300内，减少对氧化炉300的冲击。The gas to be processed enters the buffer area 101 after passing through the ventilation channel, and the buffer area 101 slows down the flow velocity of the gas, so that it enters the oxidation furnace 300 more gently, reducing the impact on the oxidation furnace 300 .
本实施例中，过滤层130的周缘侧壁与通风道的内壁相抵接，也可以理解为，过滤层130的周缘与壳体110及隔板相抵接。多个过滤层130平行设置，并且多个过滤层130与通风方向垂直。这样，令待处理气体过滤更加彻底。In this embodiment, the peripheral sidewall of the filter layer 130 is in contact with the inner wall of the air channel, which can also be understood as that the peripheral edge of the filter layer 130 is in contact with the casing 110 and the partition. Multiple filter layers 130 are arranged in parallel, and the multiple filter layers 130 are perpendicular to the ventilation direction. In this way, the gas to be treated can be filtered more thoroughly.
其他实施例中，过滤层130也可以一侧与通风道抵接，另一侧与通风道的内壁间隔设置。或者过滤层130也可以与通风方向形成锐角，例如60度等。In other embodiments, one side of the filter layer 130 may be in contact with the air channel, and the other side may be spaced apart from the inner wall of the air channel. Alternatively, the filter layer 130 may also form an acute angle with the ventilation direction, such as 60 degrees.
进一步的，过滤层130包括过滤网，以及设置于过滤网上用于过滤的功能层。具体的，过滤网围成过滤腔，功能层容置于过滤腔内。本实施例中，多个过滤层130结构相同，规格相同。Further, the filter layer 130 includes a filter net, and a functional layer disposed on the filter net for filtering. Specifically, the filter screen forms a filter cavity, and the functional layer is accommodated in the filter cavity. In this embodiment, the plurality of filter layers 130 have the same structure and the same specification.
其他实施例中，多个过滤层130也可以结构相异，例如，过滤网上的网孔规格相异，并且功能层材料相异。又如，多个功能层的厚度相异，且自过滤进风口111到过滤出风口112方向，厚度逐渐增加。此外，每个过滤层130也可以包括多个功能层。In other embodiments, the multiple filter layers 130 may also have different structures, for example, the mesh sizes on the filter screens are different, and the materials of the functional layers are different. In another example, the thicknesses of the multiple functional layers are different, and the thicknesses gradually increase from the filter air inlet 111 to the filter air outlet 112 . In addition, each filter layer 130 may also include multiple functional layers.
请一并参阅图8，其为图1所示转轮吸附浓缩RTO废气处理系统10热交换设备400的结构示意图。Please also refer to FIG. 8 , which is a schematic structural diagram of the heat exchange equipment 400 of the rotary adsorption concentration RTO waste gas treatment system 10 shown in FIG. 1 .
热交换设备400包括热交换器410、循环加热部420以及加热区域430。其中，热交换器410与氧化炉300的出风口311B、以及轮转设备的冷却区213相连接，用于热量转换，本实施例中，热交换器410为水汽热交换器410。循环加热部420与热交换器410相连接，以使热交换器410为循环加热部420提供热量。加热区域430与循环加热部420相连接，以使循环加热部420为加热区提供能量。The heat exchange device 400 includes a heat exchanger 410 , a circulation heating unit 420 , and a heating region 430 . Wherein, the heat exchanger 410 is connected with the air outlet 311B of the oxidation furnace 300 and the cooling zone 213 of the rotary equipment for heat conversion. In this embodiment, the heat exchanger 410 is a water vapor heat exchanger 410 . The circulation heating part 420 is connected with the heat exchanger 410 so that the heat exchanger 410 provides heat for the circulation heating part 420 . The heating zone 430 is connected to the circulation heating part 420, so that the circulation heating part 420 provides energy for the heating zone.
上述转轮吸附浓缩RTO废气处理系统10，冷却区213以及氧化炉300出风口311B中温度较高的气体能够将热量传递到热交换器410内，并进行热交换，以使其通过热交换器410后，提高热交换器410内的温度。之后热交换器410将能量传递到循环加热部420，并为循环加热部420提供能量，以减少循环加热部420加热到指定温度的需要外部的能量。最后，循环加热部420将能量传递到加热区域430，并对其加热。这样，节约了能源，令转轮吸附浓缩RTO废气处理系统10充分利用余热，节能环保。The above-mentioned rotary adsorption and concentration RTO exhaust gas treatment system 10, the gas with a higher temperature in the cooling zone 213 and the air outlet 311B of the oxidation furnace 300 can transfer heat to the heat exchanger 410 and perform heat exchange so that it passes through the heat exchanger After 410, the temperature in the heat exchanger 410 is increased. Afterwards, the heat exchanger 410 transfers the energy to the circulation heating part 420 and provides energy for the circulation heating part 420 , so as to reduce the need for external energy for heating the circulation heating part 420 to a specified temperature. Finally, the hydronic heating section 420 transfers energy to the heating zone 430 and heats it. In this way, energy is saved, and the waste heat can be fully utilized by the rotary adsorption concentration RTO waste gas treatment system 10, which is energy-saving and environment-friendly.
本实施例中，循环加热部420为恒温循环加热部420，其温度为95℃。并且，循环加热部420包括加热水箱421，以及与加热水箱421相连接的蒸汽管422，热交换器410与加热水箱421相连接。具体的，热交换器410中的高温气体为加热水箱421内的水加热，同时蒸汽管422内的气体也为加热水箱421内的水进行加热，以使循环加热部420内的温度保持在恒温。In this embodiment, the circulation heating part 420 is a constant temperature circulation heating part 420, and its temperature is 95°C. Moreover, the circulating heating part 420 includes a heating water tank 421 and a steam pipe 422 connected to the heating water tank 421 , and the heat exchanger 410 is connected to the heating water tank 421 . Specifically, the high-temperature gas in the heat exchanger 410 is heated for the water in the heating water tank 421, and the gas in the steam pipe 422 is also heated for the water in the heating water tank 421, so that the temperature in the circulating heating part 420 is maintained at a constant temperature. .
本实施例中，加热区域430为多个，多个加热区域430顺序与循环加热部420相连接，并且在循环加热部420的能量传递方向上，各加热区域430的加热温度递减。例如，加热区域430为四个，四个加热区域430的温度分别为57～60℃，55～60℃，55～60℃，29～49℃。这样，能够充分利用循环加热部420的能量为其加热。进一步的，每个加热区域430上均设有一调节阀，用于调节循环加热部420的流量，以控制热量。In this embodiment, there are a plurality of heating regions 430, and the heating regions 430 are sequentially connected to the circulation heating part 420, and the heating temperature of each heating region 430 decreases gradually in the energy transfer direction of the circulation heating part 420. For example, there are four heating regions 430 , and the temperatures of the four heating regions 430 are 57-60° C., 55-60° C., 55-60° C., and 29-49° C. respectively. In this way, the energy of the circulation heating unit 420 can be fully utilized to heat it. Further, each heating zone 430 is provided with a regulating valve for regulating the flow of the circulation heating part 420 to control the heat.
需要说明的是，多个热加热区还与交换器相连接，以循环使用能量。It should be noted that multiple thermal heating zones are also connected with exchangers to recycle energy.
需要说明的是，本实用新型的其它实施例还包括，上述各实施例中的技术特征相互组合所形成的、能够实施的废气处理系统，即转轮吸附浓缩RTO废气处理系统。It should be noted that other embodiments of the present invention also include an implementable exhaust gas treatment system formed by combining the technical features of the above-mentioned embodiments, that is, a rotary adsorption concentration RTO exhaust gas treatment system.
以上所述实施例的各技术特征可以进行任意的组合，为使描述简洁，未对上述实施例中的各个技术特征所有可能的组合都进行描述，然而，只要这些技术特征的组合不存在矛盾，都应当认为是本说明书记载的范围。The various technical features of the above-mentioned embodiments can be combined arbitrarily. For the sake of concise description, all possible combinations of the various technical features in the above-mentioned embodiments are not described. However, as long as there is no contradiction in the combination of these technical features, should be considered as within the scope of this specification.
以上所述实施例仅表达了本实用新型的几种实施方式，其描述较为具体和详细，但并不能因此而理解为对实用新型专利范围的限制。应当指出的是，对于本领域的普通技术人员来说，在不脱离本实用新型构思的前提下，还可以做出若干变形和改进，这些都属于本实用新型的保护范围。因此，本实用新型专利的保护范围应以所附权利要求为准。The above-mentioned embodiments only express several implementation modes of the utility model, and the description thereof is relatively specific and detailed, but it should not be understood as limiting the scope of the utility model patent. It should be noted that those skilled in the art can make several modifications and improvements without departing from the concept of the present invention, and these all belong to the protection scope of the present invention. Therefore, the scope of protection of the utility model patent should be based on the appended claims.
| Application Number | Priority Date | Filing Date | Title |
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| CN201520912006.6UCN205252836U (en) | 2015-11-13 | 2015-11-13 | Rotary Adsorption Concentration RTO Waste Gas Treatment System |
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520912006.6UCN205252836U (en) | 2015-11-13 | 2015-11-13 | Rotary Adsorption Concentration RTO Waste Gas Treatment System |
| Publication Number | Publication Date |
|---|---|
| CN205252836Utrue CN205252836U (en) | 2016-05-25 |
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520912006.6UActiveCN205252836U (en) | 2015-11-13 | 2015-11-13 | Rotary Adsorption Concentration RTO Waste Gas Treatment System |
| Country | Link |
|---|---|
| CN (1) | CN205252836U (en) |
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105327589A (en)* | 2015-11-13 | 2016-02-17 | 惠州市环发环保科技有限公司 | Waste gas treatment system |
| CN107754556A (en)* | 2017-11-29 | 2018-03-06 | 西安昱昌环境科技有限公司 | A kind of paint industry VOCs processing units |
| CN108452637A (en)* | 2017-02-17 | 2018-08-28 | 杰智环境科技股份有限公司 | Serial-type rotating wheel high-efficiency purification system and serial-type rotating wheel high-efficiency purification method |
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105327589A (en)* | 2015-11-13 | 2016-02-17 | 惠州市环发环保科技有限公司 | Waste gas treatment system |
| CN108452637A (en)* | 2017-02-17 | 2018-08-28 | 杰智环境科技股份有限公司 | Serial-type rotating wheel high-efficiency purification system and serial-type rotating wheel high-efficiency purification method |
| CN107754556A (en)* | 2017-11-29 | 2018-03-06 | 西安昱昌环境科技有限公司 | A kind of paint industry VOCs processing units |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right | Effective date of registration:20190923 Address after:Room 407, Building 288, Dongcheng Section, Qifeng Road, Dongcheng Street, Dongguan City, Guangdong Province Patentee after:Guangdong Zhihuan Shengfa Environmental Protection Technology Co., Ltd. Address before:516000 two West Road, Dayawan District, Guangdong, Longhai, 309, Huizhou Patentee before:HUIZHOU HUANFA ENVIRONMENTAL SCIENCE AND TECHNOLOGY CO., LTD. |