CN108278620A - A kind of cylindrical type regenerative oxidation system - Google Patents

A kind of cylindrical type regenerative oxidation system Download PDF

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Publication number
CN108278620A
CN108278620A CN201810087569.4A CN201810087569A CN108278620A CN 108278620 A CN108278620 A CN 108278620A CN 201810087569 A CN201810087569 A CN 201810087569A CN 108278620 A CN108278620 A CN 108278620A
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regenerative
valve
regenerator
cylindrical type
exhaust
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陈大龙
胡晓东
王波
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Nantong Sanxin Plastics Equipment Technology Co Ltd
University of Shanghai for Science and Technology
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Nantong Sanxin Plastics Equipment Technology Co Ltd
University of Shanghai for Science and Technology
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • F23G7/061Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
    • F23G7/065Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel
    • F23G7/066Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel preheating the waste gas by the heat of the combustion, e.g. recuperation type incinerator
    • F23G7/068Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel preheating the waste gas by the heat of the combustion, e.g. recuperation type incinerator using regenerative heat recovery means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2206/00Waste heat recuperation
    • F23G2206/10Waste heat recuperation reintroducing the heat in the same process, e.g. for predrying
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2209/00Specific waste
    • F23G2209/14Gaseous waste or fumes

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  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Incineration Of Waste (AREA)

Abstract

本发明公开了一种圆柱型蓄热氧化系统,包括圆柱型七室蓄热氧化炉,圆柱型七室蓄热氧化炉包括均匀分布在圆柱体内的七个伞形区域的蓄热室,分别为蓄热室一、蓄热室二、蓄热室三、蓄热室四、蓄热室五、蓄热室六、蓄热室七,圆柱型七室蓄热氧化炉接进车间废气和空气,圆柱型七室蓄热氧化炉的排气处连接有热能回收系统,热能回收系统排气处连接有烟囱,圆柱型七室蓄热氧化炉的排气处连接烟囱,圆柱型七室蓄热氧化炉内安装有气体燃烧器。本发明的优点在于:通过空气补入和辅助加热装置,并将圆柱型七室蓄热氧化炉七室中的一室,是上一循环中的第一个废气进入的室,设置循环管,进一步消除阀门换向时烟气中携带的微量VOC,使排出的废气达到排放标准。

The invention discloses a cylindrical thermal storage oxidation system, which comprises a cylindrical seven-chamber thermal storage oxidation furnace. The cylindrical seven-chamber thermal storage oxidation furnace includes seven umbrella-shaped regenerators evenly distributed in the cylindrical body, which are respectively Regenerator 1, Regenerator 2, Regenerator 3, Regenerator 4, Regenerator 5, Regenerator 6, Regenerator 7, the cylindrical seven-chamber regenerative oxidation furnace is connected to the waste gas and air of the workshop, The exhaust of the cylindrical seven-chamber thermal storage oxidation furnace is connected to a heat recovery system, and the exhaust of the heat recovery system is connected to a chimney. The exhaust of the cylindrical seven-chamber thermal storage oxidation furnace is connected to the chimney. A gas burner is installed in the furnace. The advantages of the present invention are: through the air supply and auxiliary heating device, one of the seven chambers of the cylindrical seven-chamber regenerative oxidation furnace is the first chamber where the waste gas enters in the previous cycle, and a circulation pipe is set. Further eliminate the trace amount of VOC carried in the flue gas when the valve is reversing, so that the exhaust gas can meet the emission standard.

Description

一种圆柱型蓄热氧化系统A cylindrical thermal storage oxidation system

技术领域technical field

本发明涉及VOCs废气处理技术领域,特别涉及一种圆柱型蓄热氧化系统。The invention relates to the technical field of VOCs waste gas treatment, in particular to a cylindrical thermal storage oxidation system.

背景技术Background technique

挥发性有机物VOCs是一类有机化合物总称,在美国EPA优先控制187种污染物中有33种属于VOCs,在我国VOCs已作为污染物开始系统控制和防治。VOCs具多方面危害性,具体体现在:绝大部分VOCs具有刺激性气味,对人体有致癌、致畸、致突变作用,浓度过高时很容易引起急性中毒,轻者会出现头晕、咳嗽、恶心,重者可能会出现昏迷甚至会有生命危险;部分易燃易爆VOCs还会引起火灾和爆炸。由此可见,VOCs对人体乃至整个生态系统危害巨大,VOCs监测分析与控制治理是现代环境保护工作重点之一。Volatile organic compounds (VOCs) are a general term for a class of organic compounds. Among the 187 pollutants prioritized by the US EPA, 33 belong to VOCs. In my country, VOCs have been systematically controlled and prevented as pollutants. VOCs are harmful in many ways, specifically reflected in the following: most VOCs have pungent odors, and have carcinogenic, teratogenic, and mutagenic effects on the human body. When the concentration is too high, it is easy to cause acute poisoning. In mild cases, dizziness, coughing, Nausea, severe cases may lead to coma or even life-threatening; some flammable and explosive VOCs can also cause fire and explosion. It can be seen that VOCs are extremely harmful to the human body and even the entire ecosystem, and VOCs monitoring, analysis, control and governance are one of the priorities of modern environmental protection.

发明内容Contents of the invention

本发明要解决的技术问题是提供一种能够循环处理VOCs废气且能进行余热回收的圆柱型蓄热氧化系统。The technical problem to be solved by the present invention is to provide a cylindrical thermal storage oxidation system capable of recycling VOCs waste gas and recovering waste heat.

为解决上述技术问题,本发明的技术方案为:一种圆柱型蓄热氧化系统,其创新点在于:包括圆柱型七室蓄热氧化炉,所述圆柱型七室蓄热氧化炉包括均匀分布在圆柱体内的七个伞形区域的蓄热室,分别为蓄热室一、蓄热室二、蓄热室三、蓄热室四、蓄热室五、蓄热室六、蓄热室七,所述圆柱型七室蓄热氧化炉接进车间废气和空气,所述圆柱型七室蓄热氧化炉的排气处连接有热能回收系统,所述热能回收系统排气处连接有烟囱,所述圆柱型七室蓄热氧化炉的排气处连接至烟囱,所述圆柱型七室蓄热氧化炉内安装有气体燃烧器。In order to solve the above technical problems, the technical solution of the present invention is: a cylindrical thermal storage oxidation system, the innovation point of which is that it includes a cylindrical seven-chamber thermal storage oxidation furnace, and the cylindrical seven-chamber thermal storage oxidation furnace includes uniformly distributed The regenerators in the seven umbrella-shaped areas in the cylinder are regenerator 1, regenerator 2, regenerator 3, regenerator 4, regenerator 5, regenerator 6 and regenerator 7 , the cylindrical seven-chamber thermal storage oxidation furnace is connected to workshop exhaust gas and air, the exhaust of the cylindrical seven-chamber thermal storage oxidation furnace is connected with a heat energy recovery system, and the exhaust of the heat energy recovery system is connected with a chimney, The exhaust of the cylindrical seven-chamber thermal storage oxidation furnace is connected to a chimney, and a gas burner is installed in the cylindrical seven-chamber thermal storage oxidation furnace.

进一步的,所述每个蓄热室均连接有阀门A、阀门B和阀门C,所述七个蓄热室的阀门A相连通并与送风风机相连,所述送风风机与车间相连通,所述七个蓄热室的阀门B相连通并与烟囱相连通,所述七个蓄热室的阀门C相连通并与清扫风机相连,所述清扫风机的排气口连接至送风风机的进气口。Further, each of the regenerators is connected with a valve A, a valve B and a valve C, and the valves A of the seven regenerators are connected and connected with the air supply fan, and the air supply fan is connected with the workshop , the valves B of the seven regenerators are connected and communicated with the chimney, the valves C of the seven regenerators are connected and connected with the cleaning fan, and the exhaust port of the cleaning fan is connected to the air supply fan air intake.

进一步的,所述圆柱型七室蓄热氧化炉的上排气处安装有阀门D,所述热能回收系统的下排气处与烟囱之间安装有阀门E。Further, a valve D is installed at the upper exhaust of the cylindrical seven-chamber thermal storage oxidation furnace, and a valve E is installed between the lower exhaust of the heat recovery system and the chimney.

进一步的,所述热能回收系统连接有热水箱、冷水箱和变频水泵且构成回路。Further, the heat energy recovery system is connected with a hot water tank, a cold water tank and a frequency conversion water pump to form a circuit.

进一步的,所述变频水泵共有两个。Further, there are two variable frequency water pumps.

进一步的,所述热水箱与冷水箱直接通过溢流管连接。Further, the hot water tank is directly connected to the cold water tank through an overflow pipe.

进一步的,所述空气接进处安装有阀门F,所述车间废气接进处安装有阀门G,所述车间废气接进处还安装有用来应急排放的阀门H。Further, a valve F is installed at the inlet of the air, a valve G is installed at the inlet of the workshop exhaust gas, and a valve H for emergency discharge is installed at the inlet of the workshop exhaust gas.

进一步的,所述气体燃烧器上安装有进燃气的阀门I。Further, a gas inlet valve I is installed on the gas burner.

本发明的优点在于:The advantages of the present invention are:

(1)通过空气补入和辅助加热装置,并将圆柱型七室蓄热氧化炉七室中的一室,是上一循环中的第一个废气进入的室,设置循环管,进一步消除阀门换向时烟气中携带的微量VOC,使排出的废气达到排放标准。(1) Through the air supply and auxiliary heating device, one of the seven chambers of the cylindrical seven-chamber regenerative oxidation furnace is the first chamber where the waste gas enters in the previous cycle, and the circulation pipe is set to further eliminate the valve The trace amount of VOC carried in the flue gas during the reversing makes the exhaust gas meet the emission standard.

(2)布置热能回收系统进一步回收利用圆柱型七室蓄热氧化炉出口烟气的热量,同时处理装置在浓度流量波动较大时保持稳定。(2) Arrange the heat energy recovery system to further recover and utilize the heat of the flue gas at the outlet of the cylindrical seven-chamber regenerative oxidation furnace, and at the same time, the processing device remains stable when the concentration and flow fluctuate greatly.

(3)与其他的旋转式蓄热氧化炉先进的是使用阀门进行切换,并用管道连接,提高了耐用性、密封性与可靠性及维护保养简单,设计的体积可随意大小。(3) Compared with other rotary regenerative oxidation furnaces, it is more advanced to use valves to switch and connect with pipes, which improves durability, sealing and reliability, and is easy to maintain. The designed volume can be of any size.

附图说明Description of drawings

下面结合附图和具体实施方式对本发明作进一步详细的说明。The present invention will be further described in detail below in conjunction with the accompanying drawings and specific embodiments.

图1为本发明一种圆柱型蓄热氧化系统的结构示意图。Fig. 1 is a structural schematic diagram of a cylindrical thermal storage oxidation system of the present invention.

具体实施方式Detailed ways

下面的实施例可以使本专业的技术人员更全面地理解本发明,但并不因此将本发明限制在所述的实施例范围之中。The following examples can enable those skilled in the art to understand the present invention more comprehensively, but the present invention is not limited to the scope of the described examples.

如图1所示,一种圆柱型蓄热氧化系统,包括圆柱型七室蓄热氧化炉,圆柱型七室蓄热氧化炉包括均匀分布在圆柱体内的七个伞形区域的蓄热室,分别为蓄热室一1、蓄热室二2、蓄热室三3、蓄热室四4、蓄热室五5、蓄热室六6、蓄热室七7,圆柱型七室蓄热氧化炉接进车间废气和空气,空气接进处安装有阀门F8,车间废气接进处安装有阀门G9,车间废气接进处还安装有用来应急排放的阀门H10。As shown in Figure 1, a cylindrical regenerative oxidation system includes a cylindrical seven-chamber regenerative oxidation furnace, and the cylindrical seven-chamber regenerative oxidation furnace includes seven umbrella-shaped regenerators evenly distributed in the cylinder, They are regenerator one 1, regenerator two 2, regenerator three 3, regenerator four 4, regenerator five 5, regenerator six 6, regenerator seven 7, cylindrical seven-chamber heat storage The oxidation furnace is connected to the exhaust gas and air of the workshop, and the valve F8 is installed at the inlet of the air, the valve G9 is installed at the inlet of the workshop exhaust gas, and the valve H10 for emergency discharge is installed at the inlet of the workshop exhaust gas.

圆柱型七室蓄热氧化炉的排气处连接有热能回收系统11,热能回收系统11排气处连接有烟囱12,热能回收系统11连接有热水箱13、冷水箱14和变频水泵15且构成回路,变频水泵共有两个,热水箱13与冷水箱14直接通过溢流管16连接,圆柱型七室蓄热氧化炉的排气处连接至烟囱12,圆柱型七室蓄热氧化炉内安装有气体燃烧器17,气体燃烧器17上安装有进燃气的阀门I18,圆柱型七室蓄热氧化炉的上排气处安装有阀门D19,热能回收系统11的下排气处与烟囱12之间安装有阀门E20。The exhaust of the cylindrical seven-chamber thermal storage oxidation furnace is connected with a heat energy recovery system 11, the exhaust of the heat energy recovery system 11 is connected with a chimney 12, and the heat energy recovery system 11 is connected with a hot water tank 13, a cold water tank 14 and a frequency conversion water pump 15 and To form a circuit, there are two frequency conversion water pumps. The hot water tank 13 and the cold water tank 14 are directly connected through the overflow pipe 16. The exhaust of the cylindrical seven-chamber thermal storage oxidation furnace is connected to the chimney 12. The cylindrical seven-chamber thermal storage oxidation furnace A gas burner 17 is installed inside, and a gas inlet valve I18 is installed on the gas burner 17, a valve D19 is installed on the upper exhaust of the cylindrical seven-chamber thermal storage oxidation furnace, and the lower exhaust of the heat recovery system 11 is connected with the chimney A valve E20 is installed between 12.

每个蓄热室均连接有阀门A21、阀门B22和阀门C23,七个蓄热室的阀门A21相连通并与送风风机24相连,送风风机24与车间相连通,七个蓄热室的阀门B22相连通并与烟囱12相连通,七个蓄热室的阀门C23相连通并与清扫风机25相连,清扫风机25的排气口连接至送风风机24的进气口。Each regenerator is connected with valve A21, valve B22 and valve C23. The valves A21 of the seven regenerators are connected and connected with the air supply fan 24. The air supply fan 24 is connected with the workshop. The valve B22 communicates with the chimney 12 , the valve C23 of the seven regenerators communicates with the cleaning fan 25 , and the exhaust port of the cleaning fan 25 is connected to the air inlet of the blower fan 24 .

一种圆柱型蓄热氧化系统使用如下:先开启清扫风机25进行吹风,排出炉内可能残存的可燃性物质,然后启动气体燃烧器17,对炉内蓄热体进行加热。当炉内蓄热体温度升高到指定温度后,开启车间废气接进处安装有阀门G9,向炉内通入废气,其循环工作过程包括四个周期:首先向蓄热室一1内通入废气,废气在蓄热体的加热下达到VOCs的氧化温度,VOCs分解为CO2和H2O并放出热量,蓄热室一1内蓄热体的温度逐渐下降;净化后的高温气体从蓄热室四排出,将热量传递给蓄热室四4中的蓄热体,再由烟囱排出;清扫风机25抽取新鲜空气对蓄热室七7清扫干净蓄热室七7中可能残留的VOCs,使其处于备用状态。当蓄热室一1与蓄热室四4工作后,延时30秒开启蓄热室二2内通入废气,废气从蓄热室五5内排出,当蓄热室二2与蓄热室五5工作后,延时30秒开启蓄热室三3内通入废气,废气从蓄热室六6内排出。第一个周期终了时,废气由蓄热室四4进入并预热、氧化,从蓄热室七7排出,加热蓄热室七7中的蓄热体,同时吹扫蓄热室一1,使其处于备用状态。第二个周期终了时,废气由蓄热室五5进入并预热、氧化,从蓄热室一1排出,加热蓄热室一1中的蓄热体,同时吹扫蓄热室二2,使其处于备用状态。第三个周期终了时,废气由蓄热室六6进入并预热、氧化,从蓄热室二2排出,加热蓄热室二2中的蓄热体,同时吹扫蓄热室三3,使其处于备用状态。第四个周期终了时,废气由蓄热室六6进入并预热、氧化,从蓄热室三3排出,加热蓄热室三3中的蓄热体,同时吹扫蓄热室四4,使其处于备用状态。一个大周期终了,七个蓄热室如此交替工作。A cylindrical regenerative oxidation system is used as follows: firstly turn on the cleaning fan 25 to blow air, discharge the combustible substances that may remain in the furnace, and then start the gas burner 17 to heat the regenerator in the furnace. When the temperature of the regenerator in the furnace rises to the specified temperature, the valve G9 installed at the inlet of the exhaust gas in the workshop is opened, and the exhaust gas is introduced into the furnace. Into the waste gas, the waste gas reaches the oxidation temperature of VOCs under the heating of the regenerator, and the VOCs decomposes into CO 2 and H 2 O and releases heat, and the temperature of the regenerator in the regenerator 1 gradually decreases; the purified high-temperature gas from The regenerator 4 is discharged, and the heat is transferred to the regenerator in the regenerator 4, and then discharged from the chimney; the cleaning fan 25 extracts fresh air to clean the regenerator 7 to clean up the VOCs that may remain in the regenerator 7 , leaving it in a standby state. After the regenerator one 1 and the regenerator four 4 work, delay 30 seconds to open the regenerator two 2 to feed the exhaust gas, and the exhaust gas is discharged from the regenerator five 5, when the regenerator two 2 and the regenerator After 5 5 works, delay 30 seconds to open the regenerator 3 3 to feed waste gas, and the waste gas is discharged from the regenerator 6 6 . At the end of the first cycle, the waste gas enters from the regenerator 4 4 and is preheated and oxidized, and is discharged from the regenerator 7 7 to heat the regenerator in the regenerator 7 7 and purge the regenerator 1 at the same time. put it on standby. At the end of the second cycle, the exhaust gas enters from the regenerator 5 5 and is preheated and oxidized, and is discharged from the regenerator 1 1 to heat the regenerator in the regenerator 1 , while purging the regenerator 2 . put it on standby. At the end of the third cycle, the exhaust gas enters the regenerator six 6 and is preheated and oxidized, and is discharged from the regenerator two 2 to heat the regenerator in the regenerator two 2 and purge the regenerator three 3 at the same time. put it on standby. At the end of the fourth cycle, the exhaust gas enters the regenerator six 6 and is preheated and oxidized, and is discharged from the regenerator three 3 to heat the regenerator in the regenerator three 3 and purge the regenerator four 4 at the same time. put it on standby. A big cycle ends, and the seven regenerators work alternately in this way.

当废气中VOCs浓度升高,导致燃烧室温度偏高时,部分烟气直接通过热能回收系统11减温后由烟囱排出,减少蓄热体蓄积的热量,降低废气预热温度。When the concentration of VOCs in the exhaust gas increases, resulting in a high temperature in the combustion chamber, part of the flue gas is directly discharged from the chimney after cooling through the heat energy recovery system 11, reducing the heat accumulated in the heat storage body and reducing the preheating temperature of the exhaust gas.

当废气中VOCs浓度较低时,导致燃烧室温度偏低时,启动气体燃烧器17补充热量,以保持炉内温度稳定。When the concentration of VOCs in the waste gas is low and the temperature of the combustion chamber is low, start the gas burner 17 to supplement the heat to keep the temperature in the furnace stable.

当发生燃烧室超温、设备故障及其它紧急事故时,切断车间废气接进处的阀门G9,开启用来应急排放的阀门H10。In the event of over-temperature of the combustion chamber, equipment failure and other emergencies, cut off the valve G9 at the inlet of the waste gas in the workshop, and open the valve H10 for emergency discharge.

以上显示和描述了本发明的基本原理和主要特征以及本发明的优点。本行业的技术人员应该了解,本发明不受上述实施例的限制,上述实施例和说明书中描述的只是说明本发明的原理,在不脱离本发明精神和范围的前提下,本发明还会有各种变化和改进,这些变化和改进都落入要求保护的本发明范围内。本发明要求保护范围由所附的权利要求书及其等效物界定。The basic principles and main features of the present invention and the advantages of the present invention have been shown and described above. Those skilled in the industry should understand that the present invention is not limited by the above-mentioned embodiments, and what described in the above-mentioned embodiments and the description only illustrates the principles of the present invention, and the present invention will also have other functions without departing from the spirit and scope of the present invention. Variations and improvements all fall within the scope of the claimed invention. The protection scope of the present invention is defined by the appended claims and their equivalents.

Claims (8)

1. a kind of cylindrical type regenerative oxidation system, it is characterised in that:Including seven Room regenerative oxidation stove of cylindrical type, the cylindrical type seven Room regenerative oxidation stove includes the regenerative chamber for seven pileated regions being evenly distributed in cylinder, respectively regenerative chamber one, accumulation of heat Room two, regenerative chamber three, regenerative chamber four, regenerative chamber five, regenerative chamber six, regenerative chamber seven, seven Room regenerative oxidation stove of the cylindrical type connect Into house exhaust and air, heat reclaiming system, the thermal energy are connected at the exhaust of seven Room regenerative oxidation stove of the cylindrical type It is connected with chimney at recovery system exhaust, chimney, the cylinder are connected at the exhaust of seven Room regenerative oxidation stove of the cylindrical type Gas burner is installed in seven Room regenerative oxidation stove of type.
2. a kind of cylindrical type regenerative oxidation system according to claim 1, it is characterised in that:Each regenerative chamber connects It is connected to valve A, valve B and valve C, the valve A of seven regenerative chambers is connected and is connected with breeze fan, the air-supply wind Machine is connected with workshop, and the valve B of seven regenerative chambers is connected and is connected with chimney, the valve of seven regenerative chambers C is connected and is connected with wind turbine is cleaned, and the exhaust outlet for cleaning wind turbine is connected to the air inlet of breeze fan.
3. a kind of cylindrical type regenerative oxidation system according to claim 2, it is characterised in that:Seven Room accumulation of heat of the cylindrical type Valve D is installed at the upper exhaust of oxidation furnace, valve E is installed between chimney at the lower exhaust of the heat reclaiming system.
4. a kind of cylindrical type regenerative oxidation system according to claim 3, it is characterised in that:The heat reclaiming system connects It is connected to boiler, cold water storage cistern and variable frequency pump and constitutes circuit.
5. a kind of cylindrical type regenerative oxidation system according to claim 4, it is characterised in that:The variable frequency pump shares two It is a.
6. a kind of cylindrical type regenerative oxidation system according to claim 5, it is characterised in that:The boiler and cold water storage cistern Directly connected by overflow pipe.
7. a kind of cylindrical type regenerative oxidation system according to claim 6, it is characterised in that:The air place of the tapping into installation There are valve F, the house exhaust place of tapping into that valve G is installed, the house exhaust place of tapping into is also equipped with for emergent discharge Valve H.
8. a kind of cylindrical type regenerative oxidation system according to claim 7, it is characterised in that:Pacify on the gas burner Equipped with the valve I into combustion gas.
CN201810087569.4A 2018-01-30 2018-01-30 A kind of cylindrical type regenerative oxidation system Pending CN108278620A (en)

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CN118499793A (en) * 2024-05-06 2024-08-16 安徽迈恩能源科技有限公司 Low temperature methanol scrubbing of CO2Multi-pollutant cooperative treatment equipment and process for tail gas

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CN205878190U (en) * 2016-08-03 2017-01-11 天元康宇(天津)环保科技股份有限公司 Heat accumulation formula heating power oxidation equipment
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CN201779670U (en) * 2010-09-05 2011-03-30 江苏金能环境科技有限公司 One-box multi-chamber heat accumulation incinerator with heat recovery function
CN202382258U (en) * 2011-12-15 2012-08-15 柯鹏鸿 Heat accumulating type high-temperature oxidation furnace
CN104344409A (en) * 2013-08-07 2015-02-11 上海同济华康环境科技有限公司 Method for processing exhaust gas containing high-concentration organic pollutant
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* Cited by examiner, † Cited by third party
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CN109373773A (en) * 2018-09-27 2019-02-22 中冶华天工程技术有限公司 Furnace continuous heat exchange control device and control method
CN118499793A (en) * 2024-05-06 2024-08-16 安徽迈恩能源科技有限公司 Low temperature methanol scrubbing of CO2Multi-pollutant cooperative treatment equipment and process for tail gas

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