WO2012070892A2 - Air intake/exhaust distribution chamber having cyclically operating valves, and regenerative thermal oxidizer comprising same - Google Patents

Air intake/exhaust distribution chamber having cyclically operating valves, and regenerative thermal oxidizer comprising same Download PDF

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Publication number
WO2012070892A2
WO2012070892A2 PCT/KR2011/009030 KR2011009030W WO2012070892A2 WO 2012070892 A2 WO2012070892 A2 WO 2012070892A2 KR 2011009030 W KR2011009030 W KR 2011009030W WO 2012070892 A2 WO2012070892 A2 WO 2012070892A2
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exhaust
heat storage
valve
valves
storage tank
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PCT/KR2011/009030
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French (fr)
Korean (ko)
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WO2012070892A3 (en
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김종석
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주식회사 태종이엔씨
김은연
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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

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  • the present invention is a device that completely processes and exhausts by burning and oxidizing harmful gases containing various odors or volatile organic compounds (VOC) generated in the industrial field, employing a heat storage tank to save more than 95% of fuel for combustion Furthermore, it is a device to treat harmful gases containing high concentration of volatile organic compounds (VOC) with a minimum of auxiliary fuel, and the remaining heat can be utilized as a heat source (heat, fruit boiler, etc.) in the production process. to be.
  • VOC volatile organic compounds
  • the present invention includes a supply / exhaust distribution chamber having a circulating valve, and divides the heat storage tank in which the heat storage material is stored by the number of valves and supplies noxious gas through the heat storage tank at the same time, and cleans the gas after combustion. Exhaust through the heat storage tank and purge supply is continuously crossed and changed (alternatively) to increase the efficiency of removing pollutants, while maximizing utilization efficiency while eliminating the mixing of harmful gas for treatment and clean gas after treatment.
  • Hazardous gases containing various pollutants are generated at industrial sites, and in the fields involving large-scale painting and coating processes such as shipyards, large amounts of volatile organic compounds are generated and react with light in the air to react with ozone or aldehyde or By producing photo-oxide, it causes environmental pollution such as global warming.
  • Substances that form volatile organic compounds cause irritating and unpleasant odors even at low concentrations, and when absorbed into the human body through the respiratory tract, cause nervous system disorders, some of which have carcinogenic properties. Emission restrictions are in force.
  • the legal allowable emission standard is 40ppm or less, but the concentration of exhausted from workplaces such as shipbuilding and furniture manufacturing is about 2,500 ⁇ 4,000ppm, which requires very strict treatment.
  • RTO Combustion oxidation apparatus
  • the conventional regenerative combustion oxidizer allows harmful gas to flow through a plurality of heat storage chambers filled with a heat storage material at a lower end of a combustion chamber, and in this process, preheats harmful gas for treatment by using heat stored in the heat storage material.
  • the gas reaches the combustion chamber, the gas is heated to a temperature close to the combustion temperature (700 ° C), and heat is recovered in the process of exhausting the high-temperature (800 ° C) clean gas after the combustion through the heat storage chamber again. Finally, the temperature of the clean gas discharged is maintained at a temperature of 30 ⁇ 40 °C higher than the temperature of the low-temperature gas supply.
  • inflow of harmful gas for treatment and exhaust of clean gas after treatment are alternately performed by distribution means.
  • Korean Patent Laid-Open Publication No. 2003-11036 which is located between the upper fixing plate 41 and the lower fixing plate 42 of the fixed rotating plate 40 and rotates therein, and includes an inflow passage 51. And a disk 50 and drive means 70 for rotating the disk.
  • the disk 50, the upper fixing plate 41 and the lower fixing plate 42, which are the horizontal rotating bodies of the prior art, are all made of metal and have a diameter of about 3 m (in case of a large industrial capacity), so they can be rotated for a long time.
  • the leakage occurs frequently due to the wear of the friction surface between the disk 50 and the upper and lower fixing plates 41 and 42 which are horizontal rotating bodies. Even if such leakage occurs during operation and the mixing of harmful gas for treatment and clean gas after 1 ⁇ 2% occurs, a serious problem that does not meet the exhaustion standards arises. Of course, it causes very problems that directly affect the operation of the production facility.
  • the present invention is to fundamentally solve the above-described problems of the prior art, completely excludes the mechanical disk and the driving means, and cleans them after a number of treatments such as a plurality of (2n + p) hazardous gas supply valve for treatment.
  • a regenerative combustion oxidizer which does not require a rotating body by replacing the supply / exhaust distribution chamber consisting of a gas exhaust valve.
  • the present invention is to improve the airtightness, lower the possibility of failure, compared to the conventional disk, multiple disk, drum type, and to provide a low-volume regenerative combustion oxidation apparatus.
  • the present invention is to provide a regenerative combustion oxidation apparatus that can be used by simply retrofitting the existing disk type to the valve type while providing a supply and exhaust distribution chamber having a circulation-actuated valve.
  • the present invention includes a plurality of (2n + p) n air supply valves (for heat dissipation) in the air distribution chamber, of which n is open and the rest are closed, p of the closing valves. Valves to purge.
  • n is the number of valves in charge of the air supply opening function and the number is equal to or greater than the number p of valves in charge of the purge function (n ⁇ p).
  • the exhaust distribution chamber is provided with the same number of exhaust valves (for regenerative storage), but those in the opposite position to the air supply valve are assembled so that n or n + 1 is opened and the remaining n + 1 or n are It is an invention that the heat storage and heat dissipation occur evenly in all areas of the heat storage tank divided into 2n + p areas by sequentially operating to close.
  • the present invention does not have a rotary disk, wear and tear caused by the rotational portion and the resulting leakage problem are fundamentally solved, the durability of the apparatus is significantly increased, and the possibility of violating the exhaustion standard is greatly reduced.
  • the device is simplified by excluding the rotating disk and its driving means, and the effect of reducing the energy use required to obtain the driving force is expected.
  • the regenerative combustion oxidizer having a circulating actuating valve of the present invention is provided with a combustion chamber in the upper portion of the cylinder and a lower portion thereof and is provided with 2n + p regions by a partition wall extending from the central axis to the circumference in the radial direction.
  • a heat storage tank provided at a lower portion of the heat storage tank and a heat storage tank including 2n + p air supply valves 50 corresponding to the partitioned heat storage tank to supply noxious gas to the combustion chamber through the heat storage tank.
  • a supply / exhaust distribution chamber 4 composed of an exhaust distribution chamber including the same number of exhaust valves 60 for discharging the clean gas processed therethrough.
  • one air supply valve and one exhaust valve are paired in each of the divided heat storage tanks so that the heat storage tank, the air supply valves, and the exhaust valves each have 2n + p numbers.
  • the heat storage tank is partitioned into five regions by coaxially extending partition walls.
  • the partition wall partitioning the heat storage tank may be divided into concentric circles, and may be provided to have various shapes such as a rectangular shape as necessary to minimize the size of the installation and the installation space.
  • the present invention includes five air supply valves 51 to 55 at equal intervals along the same distance in the circumferential direction from the central axis of the outer air distribution chamber, and five exhaust valves 61 to the inner exhaust distribution chamber. 65).
  • the air supply distribution chamber provided with the air supply valves 51 to 55 communicates with the inflow duct 7 and receives a harmful gas for treatment to supply the combustion chamber to the combustion chamber through the heat storage tank, and the exhaust valves 61 to 65 are provided.
  • the distribution chamber communicates with the exhaust duct 8 to exhaust the treated clean gas into the atmosphere.
  • the air distribution chamber and the exhaust distribution chamber are divided into spaces by a housing having concentric partitions, which are well known as shown in FIG.
  • the five-stage heat storage tank operates in order to maintain the temperature uniformly in all regions by repeating heat radiation and heat storage sequentially.
  • the present invention is provided with a control means (not shown) for operating the air supply valve and the exhaust valve in accordance with the above operation sequence, it is preferable that the provided valves are provided with an electronic valve that operates in accordance with the electrical signal.
  • each of the valves is sequentially operated so that each of n supply and exhaust air is opened, n supply air and n + 1 exhaust gas are closed, and one supply air is purged.
  • the purge is not operated to the combustion chamber from the heat storage tank section connected to the air supply valve, which is opened for the first time, and the remaining gas is not directly discharged to the exhaust side, and is sent back to the front of the air supply valve. do.
  • all the valves are provided in order to rotate indefinitely alternately.
  • FIG. 6 is a pre-heating and cooling of the corresponding heat storage tank is supplied as the harmful gas for treatment is supplied along the heat storage tank compartment arranged on the left side according to the operation of the first stage valve, and simultaneously cleaned after heating along the heat storage tank compartment arranged on the right side. As the gas is exhausted, heat accumulation in the heat storage tank and cooling of the exhaust gas are shown.
  • 6 and 7 is a pre-heating and cooling of the corresponding heat storage tank is supplied as the harmful gas for treatment is supplied along the heat storage tank compartment arranged on the right side according to the operation of the two-stage valve, and simultaneously cleaned after heating along the heat storage tank compartment arranged on the left side.
  • 6 and 7 are provided with a purge valve 11 in accordance with the purge operation of the air supply valves 51 to 55 in sequence to guide the harmful gas remaining in the pipe connected to the air supply valve to the air supply side untreated pollution Prevent residual gas from being discharged to the atmosphere along the exhaust line.
  • the three to five stage valves operate according to the same principle to switch the supply and exhaust zones sequentially so that all areas of the five compartments of the heat storage tank are kept at a uniform temperature.
  • the regenerative combustion oxidation apparatus of the present invention is provided with a blower at the inlet side of the inlet duct (7), and further includes a bypass pipe (10) directly connected to the chimney from the combustion chamber in order to prevent the high temperature of the combustion chamber.
  • the regenerative combustion oxidizer of the present invention includes a valve type supply / exhaust distribution chamber.
  • the upper and lower fixed plates 41 and 42 and the horizontal rotating plate 50 are provided. It is possible to easily modify and use the existing equipment in a way to replace the fixed passage 40 made of the valve-type supply and exhaust distribution structure of the present invention. At this time, the existing compartment heat storage tank and the combustion chamber can be utilized as it is.

Abstract

The aim of the present invention is to fundamentally solve leakage problems caused by an abrasion of rotating portions of conventional rotating disk-type regenerative thermal oxidizers. The regenerative thermal oxidizer of the present invention comprises an air intake/exhaust distribution chamber having cyclically operating valves, and is configured such that a thermal storage tank having a thermal storage material stored therein is divided into sections corresponding to the number of valves. Thus, noxious gases are supplied through a section of the thermal storage tank, and clean gases obtained after combustion are exhausted through another section of the thermal storage tank. In addition, the supply of purge gases is continuously and alternately performed to improve the efficiency of removing contaminants. As a result, the efficiency of using the regenerative thermal oxidizer is maximized while fundamentally preventing noxious gases before treatment and clean gases after treatment from being mixed.

Description

순환 작동형 밸브를 구비한 급배기 분배실과 이를 구비한 축열식 연소산화장치Supply / exhaust distribution chamber with circulating valve and regenerative combustion oxidizer
본 발명은 산업현장에서 발생하는 각종 악취 또는 휘발성유기화합물(VOC) 등이 함유된 유해가스를 연소 및 산화시켜 완벽하게 처리하여 배기하는 장치로서, 축열조를 채용하여 연소용 연료를 95% 이상 절약하고, 더 나아가서 고농도의 휘발성유기화합물(VOC)이 함유된 유해가스를 보조연료를 최소한으로 사용하여 처리하며, 이 때 남는 열량은 생산공정 등에 열원(열품, 열매 보일러 등)으로 활용할 수 있도록 하기 위한 장치이다. The present invention is a device that completely processes and exhausts by burning and oxidizing harmful gases containing various odors or volatile organic compounds (VOC) generated in the industrial field, employing a heat storage tank to save more than 95% of fuel for combustion Furthermore, it is a device to treat harmful gases containing high concentration of volatile organic compounds (VOC) with a minimum of auxiliary fuel, and the remaining heat can be utilized as a heat source (heat, fruit boiler, etc.) in the production process. to be.
상세히 보면 본 발명은 순환 작동형 밸브를 구비한 급배기 분배실을 구비하고, 축열재가 저장된 축열조를 밸브의 숫자 만큼 구획하여 유해가스를 구획된 축열조를 통해 공급함과 동시에 연소 후 청정가스를 다른 구획의 축열조를 통해 배기하며, 오염물질 제거효율을 높이기 위해 퍼지 공급이 연속적으로 교차·가변(교번)되도록 하여 이용효율을 극대화하면서도 처리용 유해가스와 처리후 청정가스가 혼합되는것을 근원적으로 배제한 장치이다. In detail, the present invention includes a supply / exhaust distribution chamber having a circulating valve, and divides the heat storage tank in which the heat storage material is stored by the number of valves and supplies noxious gas through the heat storage tank at the same time, and cleans the gas after combustion. Exhaust through the heat storage tank and purge supply is continuously crossed and changed (alternatively) to increase the efficiency of removing pollutants, while maximizing utilization efficiency while eliminating the mixing of harmful gas for treatment and clean gas after treatment.
산업현장에서는 다양한 오염물질이 함유된 유해가스가 발생되고 있으며,이중에서도 조선소와 같은 대규모 도장 및 코팅 공정이 수반되는 분야에서는 휘발성유기화합물 등이 다량으로 발생하여 대기중에서 빛과 반응하여 오존이나 알데히드 또는 광화합산화물을 생성하므로서, 지구온난화와 같은 환경오염을 유발한다.Hazardous gases containing various pollutants are generated at industrial sites, and in the fields involving large-scale painting and coating processes such as shipyards, large amounts of volatile organic compounds are generated and react with light in the air to react with ozone or aldehyde or By producing photo-oxide, it causes environmental pollution such as global warming.
휘발성유기화합물을 이루는 물질은 낮은 농도에서도 자극적이며 불쾌한 악취를 유발시키는 한편, 호흡기를 통하여 인체내로 흡수될 경우 신경계 등의 장애를 일으키며, 이중 일부는 발암 성질을 갖고 있어 최근에는 그 배기시설에 대한 엄격한 배출규제가 시행 중이다. 예를 들어 도장시설의 경우 법적 허용 배출기준이 40ppm이하 이나, 조선, 가구 제조 등의 사업장에서 배기되는 농도는 2,500~4,000ppm 정도로 높아 매우 엄격한 처리가 필요한 실정이다.Substances that form volatile organic compounds cause irritating and unpleasant odors even at low concentrations, and when absorbed into the human body through the respiratory tract, cause nervous system disorders, some of which have carcinogenic properties. Emission restrictions are in force. For example, in the case of coating facilities, the legal allowable emission standard is 40ppm or less, but the concentration of exhausted from workplaces such as shipbuilding and furniture manufacturing is about 2,500 ~ 4,000ppm, which requires very strict treatment.
위와 같은 산업현장에서 발생한 휘발성유기화합물이 포함된 유해가스를 처리하기 위하여 고온연소 및 산화처리장치로서 직접연소장치와 촉매 연소장치 등을 사용하여 왔으며, 최근에는 연료비 절감과 오염물질 제거 효율이 우수한 축열식 연소산화장치(R.T.O)가 대표적으로 사용되고 있다.In order to treat harmful gases containing volatile organic compounds generated in the above industrial sites, direct combustion devices and catalytic combustion devices have been used as high-temperature combustion and oxidation treatment devices. Combustion oxidation apparatus (RTO) is typically used.
상기 종래의 축열식 연소산화장치는 연소실 하단부에 축열재가 충진된 다수의 축열실을 통하여 유해가스가 유입되도록 하고, 이 과정에서 축열재에 축열된 열을 이용하여 처리용 유해가스를 예열시켜 처리용 유해가스가 연소실에 도달할 때 연소 온도에 근접한 온도까지 승온(700℃)되도록 하고, 연소후 처리된 높은 온도 (800℃)의 청정가스를 다시 축열실을 통해 배기시키는 과정에서 열을 회수(축열)하며, 최종적으로 배기되는 청정가스의 온도는 저온상태의 급기가스 온도 보다 30~40℃ 높은 정도를 유지한다. 상기와 같은 종래의 축열식 연소산화장치는 처리용 유해가스의 유입 및 처리후 청정가스의 배기가 분배수단에 의하여 교대로 이루어지도록 되어 있다. The conventional regenerative combustion oxidizer allows harmful gas to flow through a plurality of heat storage chambers filled with a heat storage material at a lower end of a combustion chamber, and in this process, preheats harmful gas for treatment by using heat stored in the heat storage material. When the gas reaches the combustion chamber, the gas is heated to a temperature close to the combustion temperature (700 ° C), and heat is recovered in the process of exhausting the high-temperature (800 ° C) clean gas after the combustion through the heat storage chamber again. Finally, the temperature of the clean gas discharged is maintained at a temperature of 30 ~ 40 ℃ higher than the temperature of the low-temperature gas supply. In the conventional regenerative combustion oxidation apparatus as described above, inflow of harmful gas for treatment and exhaust of clean gas after treatment are alternately performed by distribution means.
이중 대표적인 것이 공개특허 특2003-11036호에 개시되어 있는바, 이는 고정회전판(40)의 상부고정판(41)과 하부고정판(42) 사이에 위치하여 회전하며, 유입관통부(51)을 구비한 디스크(50)와 이를 회전 구동하기 위한 구동수단(70) 등을 구비한다. 상기한 종래기술의 수평 회전체인 디스크(50)와 상부고정판(41) 및 하부고정판(42)는 모두 금속재이며, 직경이 3m(용량이 큰 산업용의 경우) 정도에 이르는 대형 구조물이므로 장기간 회전 운전시에 수평 회전체인 디스크(50)와 상하부고정판(41,42) 사이의 마찰면의 마모로 인하여 누설이 빈번하게 발생하고 있다. 이와 같은 운전 중 누설이 발생하여 처리용 유해가스와 처리후 청정가스가 1~2% 정도만 섞이는 현상이 발생하더라도 배기기준을 충족하지 못하는 심각한 문제가 대두되므로 수시로 정비 보수를 하여야 하나, 이는 비용부담은 물론, 생산설비의 가동에 직접적으로 중대한 지장을 초래하는 매우 문제를 유발한다. A representative one of them is disclosed in Korean Patent Laid-Open Publication No. 2003-11036, which is located between the upper fixing plate 41 and the lower fixing plate 42 of the fixed rotating plate 40 and rotates therein, and includes an inflow passage 51. And a disk 50 and drive means 70 for rotating the disk. The disk 50, the upper fixing plate 41 and the lower fixing plate 42, which are the horizontal rotating bodies of the prior art, are all made of metal and have a diameter of about 3 m (in case of a large industrial capacity), so they can be rotated for a long time. The leakage occurs frequently due to the wear of the friction surface between the disk 50 and the upper and lower fixing plates 41 and 42 which are horizontal rotating bodies. Even if such leakage occurs during operation and the mixing of harmful gas for treatment and clean gas after 1 ~ 2% occurs, a serious problem that does not meet the exhaustion standards arises. Of course, it causes very problems that directly affect the operation of the production facility.
실제로 초기 가동시에 오염물질 제거효율 98% 수준을 유지하던 것이 가동시간이 경과함에 따라 디스크(50)와 상하부고정판(41,42) 사이가 급속히 마모되어 불과 수개월내에 오염물질 제거효율이 3%P이상 저하되어 매년 교체· 보수를 해야 하는 문제가 대두되고 있고, 이러한 마모 문제를 해결하기 위하여 디스크와 상하부 고정판의 간격을 여유있게 할 경우 그 자체로 기밀성이 떨어지는 근원적인 한계가 있다. In fact, the 98% level of pollutant removal efficiency during initial operation was rapidly worn out between the disk 50 and the upper and lower fixing plates 41 and 42 as the operation time passed, resulting in a 3% P removal efficiency in just a few months. As a result, the problem of having to replace and repair each year is rising, and when the space between the disc and the upper and lower fixing plates is left in order to solve such abrasion problem, there is a fundamental limitation that the airtightness itself is inferior.
본 발명은 상기한 종래기술의 문제점을 근원적으로 해결하고자 하는 것으로, 기계적인 디스크와 구동수단을 완전히 배제하고, 이를 복수개(2n+p)의 처리용 유해가스 급기용 밸브와 같은 수의 처리 후 청정가스 배기용 밸브로 이루어진 급배기 분배실로 대체하여 회전체가 필요 없는 축열식 연소산화장치를 제공하고자 한다. The present invention is to fundamentally solve the above-described problems of the prior art, completely excludes the mechanical disk and the driving means, and cleans them after a number of treatments such as a plurality of (2n + p) hazardous gas supply valve for treatment. In order to provide a regenerative combustion oxidizer which does not require a rotating body by replacing the supply / exhaust distribution chamber consisting of a gas exhaust valve.
또한, 본 발명은 종래의 디스크, 다중 디스크, 드럼형에 비하여 기밀성을 향상하고, 고장발생 가능성을 낮추며, 부피가 작은 축열식 연소산화장치를 제공하고자 한다.In addition, the present invention is to improve the airtightness, lower the possibility of failure, compared to the conventional disk, multiple disk, drum type, and to provide a low-volume regenerative combustion oxidation apparatus.
본 발명은 순환 작동형 밸브를 구비한 급배기 분배실을 제공함과 동시에 기존에 가동중인 디스크형을 밸브형으로 간단히 개조하여 사용할 수 있는 축열식 연소산화장치를 제공하고자 한다.The present invention is to provide a regenerative combustion oxidation apparatus that can be used by simply retrofitting the existing disk type to the valve type while providing a supply and exhaust distribution chamber having a circulation-actuated valve.
상기한 해결과제를 실현하기 위하여 본 발명은 급기분배실에 복수개(2n+p)n개의 급기용 밸브(방열용)를 구비하되, 이중 n개는 개방하고, 나머지는 폐쇄하며, 폐쇄밸브 중 p개의 밸브는 퍼지한다.In order to realize the above problem, the present invention includes a plurality of (2n + p) n air supply valves (for heat dissipation) in the air distribution chamber, of which n is open and the rest are closed, p of the closing valves. Valves to purge.
여기서 n은 급기 열림기능을 담당하는 밸브의 수이며 그 수는 퍼지 기능을 담당하는 밸브의 수(p) 보다 같거나 많게 구비된다(n≥p). Where n is the number of valves in charge of the air supply opening function and the number is equal to or greater than the number p of valves in charge of the purge function (n ≧ p).
이에 대응하여 배기분배실에 같은 수의 배기용 밸브(축열용)를 구비하되, 급기용 밸브와 대향위치에 있는 것들이 조를 이루어 n 또는 n+1개는 개방하고 나머지 n+1 또는 n개는 폐쇄하도록 순차적으로 교번 작동되도록 하여 2n+p개의 영역으로 구획된 축열조의 모든 영역에 있어서 축열과 방열이 고르게 일어나도록 하는 발명이다. Correspondingly, the exhaust distribution chamber is provided with the same number of exhaust valves (for regenerative storage), but those in the opposite position to the air supply valve are assembled so that n or n + 1 is opened and the remaining n + 1 or n are It is an invention that the heat storage and heat dissipation occur evenly in all areas of the heat storage tank divided into 2n + p areas by sequentially operating to close.
이때 모든 급기밸브는 개방→퍼지(폐쇄)→폐쇄→개방의 순서로 무환 순환하여 순차적으로 작동하고, 배기밸브는 개방→페쇄→개방 순서로 무환 순환하여 순차적으로 작동한다.At this time, all of the air supply valves are operated in a sequential order by circulating in the order of opening → purging (close) → closing → opening.
상기한 본 발명은 회전 디스를 구비하지 않음으로 인하여 회전부분에서 발생하는 마모와 이로 인한 누설 문제가 근원적으로 해소되어, 장치의 내구성이 현저하게 증대되고, 배기기준을 위반할 가능성이 크게 줄어든다.Since the present invention does not have a rotary disk, wear and tear caused by the rotational portion and the resulting leakage problem are fundamentally solved, the durability of the apparatus is significantly increased, and the possibility of violating the exhaustion standard is greatly reduced.
또한, 회전 디스크 및 이의 구동수단을 배제하여 장치가 단순해 지고, 구동력을 얻는데 필요한 에너지 사용을 절감하는 효과가 기대된다. In addition, the device is simplified by excluding the rotating disk and its driving means, and the effect of reducing the energy use required to obtain the driving force is expected.
운전기간의 경과에도 불구하고 운전초기 오염물질 제거효율(99% 수준)이 지속적으로 유지되는 효과가 기대된다. In spite of the passage of the operation period, it is expected that the initial efficiency of pollutant removal (99% level) will be maintained continuously.
기존에 설치 운전중인 회전 디스크형 장치의 급배기 분배실을 본 발명의 밸브를 채용한 급배기 분배실로 개조하는 방법으로 용이하게 설비를 개량할 수 있는 효과가 있다. There is an effect that can be easily improved by the method of converting the supply and exhaust distribution chamber of the rotating disk-type device in the existing installation operation to the supply and exhaust distribution chamber employing the valve of the present invention.
도1. 종래기술의 구성도Figure 1. Structure diagram of the prior art
도2. 종래기술의 가변부의 분해사시도Figure 2. Exploded perspective view of a variable part of the prior art
도3. 본 발명에 따른 시스템 분해 구성도Figure 3. System decomposition diagram according to the present invention
도4. 본 발명에 따른 밸브 배치 평면도Figure 4. Valve arrangement plan according to the invention
도5. 본 발명에 따른 밸브 배치 사시도와 밸브 작동 순서 설명도Figure 5. Illustration showing the arrangement of the valve according to the present invention and the operation sequence of the valve
도6. 본 발명의 급기 및 배기 상태도 1Figure 6. Supply and exhaust state diagram of the present invention 1
도7. 본 발명의 급기 및 배기 상태도 2Figure 7. Supply and exhaust state diagram of the present invention 2
<도면의 주요부문에 대한 부호 설명><Description of Signs of Major Sectors in Drawings>
3 연소실, 4 급배기 분배실, 5 축열조3 combustion chamber, 4 exhaust distribution chamber, 5 heat storage tank
7 유입덕트 8 배기덕트 10 바이패스관 11 퍼지 밸브7 Inlet duct 8 Exhaust duct 10 Bypass pipe 11 Purge valve
51,52,53,54,55 급기밸브 61,62,63,64,65 배기밸브51,52,53,54,55 Supply valve 61,62,63,64,65 Exhaust valve
상기한 본 발명의 목적을 달성하기 위한 구체적인 실시예로서 첨부도면을 통해 상세하게 설명한다.As a specific embodiment for achieving the above object of the present invention will be described in detail through the accompanying drawings.
도3에 의하면, 본 발명의 순환 작동형 밸브를 구비한 축열식 연소산화장치는 원통형으로 이루어진 상부의 연소실과 그 하부에 구비되며 중심축으로부터 방사방향으로 원주까지 연장된 격벽에 의해 2n+p개의 영역으로 구획된 축열조와 상기 축열조 하부에 구비되며, 축열조를 통해 연소실로 유해가스를 공급하기 위하여 상기 구획된 축열조와 대응하는 2n+p개의 급기밸브(50)를 포함하는 급기분배실과 상기 연소실로부터 축열조를 통해 처리된 청정가스를 배출하기 위한 같은 수의 배기 밸브(60)를 포함하는 배기분배실로 이루어진 급배기 분배실(4)를 포함한다. According to Fig. 3, the regenerative combustion oxidizer having a circulating actuating valve of the present invention is provided with a combustion chamber in the upper portion of the cylinder and a lower portion thereof and is provided with 2n + p regions by a partition wall extending from the central axis to the circumference in the radial direction. A heat storage tank provided at a lower portion of the heat storage tank and a heat storage tank including 2n + p air supply valves 50 corresponding to the partitioned heat storage tank to supply noxious gas to the combustion chamber through the heat storage tank. And a supply / exhaust distribution chamber 4 composed of an exhaust distribution chamber including the same number of exhaust valves 60 for discharging the clean gas processed therethrough.
이로서 구획된 축열조의 개별 영역 마다 하나의 급기밸브와 하나의 배기밸브가 짝을 이루어 축열조, 급기밸브, 배기밸브 각각이 2n+p개의 수 만큼 구비되는 것이 바람직하다.As a result, it is preferable that one air supply valve and one exhaust valve are paired in each of the divided heat storage tanks so that the heat storage tank, the air supply valves, and the exhaust valves each have 2n + p numbers.
축열조 구획 수, 급기밸브와 배기밸브는 처리용량과 정밀도를 고려하여 그 수량을 정하되, 이들 3종류의 구성요소는 공히 5개, 7개, 9개(p=1 기준) 등 같은 수량을 구비하는 것이 설비 최적화면에서 바람직하지다. 다만, 이들 3종류의 구성요소가 반드시 같은 수를 갖는 것으로 한정될 필요는 없고, 축열조의 온도를 균일하게 유지하기 위해 상호 일정한 배수 관계를 유지하는 것은 필요하다.The number of heat storage compartments, the air supply valve and the exhaust valve shall be determined in consideration of the processing capacity and precision, but these three types of components have the same quantity such as five, seven, nine (p = 1). It is desirable in terms of equipment optimization. However, these three types of components are not necessarily limited to the same number, and it is necessary to maintain a constant drainage relationship with each other in order to maintain the temperature of the heat storage tank uniformly.
도4에 도시된 바와 같이, 급기분배실과 배기분배실에 구비된 급기밸브와 배기밸브가 각각 5개(n=2, p=1)인 경우를 들어 일실시예로서 동작과정을 설명한다. As shown in FIG. 4, an operation process will be described as an example, in which five air supply valves and exhaust valves provided in the air supply distribution chamber and the exhaust distribution chamber are five (n = 2, p = 1), respectively.
이 경우 축열조는 동축 방사상으로 연장된 격벽에 의해 5개 영역으로 구획된다. 다만, 축열조를 구획하는 격벽은 동심원 형상으로 구분할 수도 있고, 설비의 크기와 설치 공간의 최소화를 위해 필요에 따라 사각형 형상 등 다양한 형상을 가지도록 구비할 수 있다. In this case, the heat storage tank is partitioned into five regions by coaxially extending partition walls. However, the partition wall partitioning the heat storage tank may be divided into concentric circles, and may be provided to have various shapes such as a rectangular shape as necessary to minimize the size of the installation and the installation space.
도4와 같이 본 발명은 외측 급기분배실에 중심축으로부터 원주방향으로 같은 거리를 따라서 동일한 간격으로 5개의 급기밸브(51~55)가 구비되고, 내측 배기분배실에는 5개의 배기밸브(61~65)가 구비된다. 상기 급기밸브(51~55)가 구비된 급기분배실은 유입덕트(7)와 연통되어 처리용 유해가스를 공급받아 축열조를 통해 연소실로 공급하고, 상기 배기밸브(61~65)가 구비된 배기분배실은 배기덕트(8)와 연통하여 처리된 청정가스를 대기중으로 배기한다. 상기 급기분배실과 배기분배실은 동심원 형상의 격벽을 갖는 하우징에 의해 공간이 분할되어 있으며, 이는 상기 종래기술 제7도에서 보는 바와 같이 공지기술이므로 더 이상의 구체적인 설명은 생략한다.As shown in Fig. 4, the present invention includes five air supply valves 51 to 55 at equal intervals along the same distance in the circumferential direction from the central axis of the outer air distribution chamber, and five exhaust valves 61 to the inner exhaust distribution chamber. 65). The air supply distribution chamber provided with the air supply valves 51 to 55 communicates with the inflow duct 7 and receives a harmful gas for treatment to supply the combustion chamber to the combustion chamber through the heat storage tank, and the exhaust valves 61 to 65 are provided. The distribution chamber communicates with the exhaust duct 8 to exhaust the treated clean gas into the atmosphere. The air distribution chamber and the exhaust distribution chamber are divided into spaces by a housing having concentric partitions, which are well known as shown in FIG.
도5는 본 발명의 밸브가 작동되는 순서를 구체적으로 설명한다. 도5는 급기밸브와 배기밸브가 각각 5개(n=2, p=1)인 경우로서, 다음과 같은 순서에 따라 작동한다. 5 specifically illustrates the order in which the valve of the present invention is operated. 5 is a case where five supply valves and five exhaust valves (n = 2, p = 1) are operated in the following order.
표 1 <배기밸브의 열림 숫자가 닫힘 숫자 보다 많은 경우>
단계 열림(급기/배기) 퍼지(급기) 닫힘(급기/배기)
1 51,52/61,62 55 53,54/63,64,65
2 52,53/62,63 51 54,55/64,65,61
3 53,54/63/64 52 55,51/65,61,62
4 54,55/64,65 53 51,52/61,62,63
5 55,51/65,61 54 52,53/62,63,64
Table 1 <When the number of open valves is greater than the number closed
step Open (air supply / exhaust) Fuzzy Air Supply Closed (air supply / exhaust)
One 51,52 / 61,62 55 53,54 / 63,64,65
2 52,53 / 62,63 51 54,55 / 64,65,61
3 53,54 / 63/64 52 55,51 / 65,61,62
4 54,55 / 64,65 53 51,52 / 61,62,63
5 55,51 / 65,61 54 52,53 / 62,63,64
위와 같은 단계별 작동 순서에 따라 5개로 구획된 축열조가 순차적으로 방열과 축열을 반복하여 모든 영역에서 균일하게 온도가 유지되도록 작동하는 것이다. 이를 위해 본 발명은 위와 같은 작동순서에 따라 급기밸브와 배기밸브를 작동시키기 위한 제어수단(미도시)이 구비되며, 구비되는 밸브들은 전기신호에 따라 동작하는 전자식 밸브로 구비함이 바람직하다. 상기 실시예는 급배기 각 n개씩 열리고, 급기 n개와 배기 n+1개가 닫히며, 급기 1개는 퍼지 동작을 하도록 모든 밸브가 순차적으로 교번 작동하는 것을 설명한다. 이때 퍼지는 열렸다가 최초로 닫히는 급기밸브와 연결된 축열조 구획에서 연소실로 공급되지 못하고 잔류된 가스가 배기측으로 바로 배출되지 못하도록 하고 이를 급기밸브 전단으로 다시 보내는 동작인바, 편의상 급기밸브를 중심으로 퍼지 동작을 설명하고자 한다. According to the step-by-step operation sequence as described above, the five-stage heat storage tank operates in order to maintain the temperature uniformly in all regions by repeating heat radiation and heat storage sequentially. To this end, the present invention is provided with a control means (not shown) for operating the air supply valve and the exhaust valve in accordance with the above operation sequence, it is preferable that the provided valves are provided with an electronic valve that operates in accordance with the electrical signal. The above embodiment explains that each of the valves is sequentially operated so that each of n supply and exhaust air is opened, n supply air and n + 1 exhaust gas are closed, and one supply air is purged. At this time, the purge is not operated to the combustion chamber from the heat storage tank section connected to the air supply valve, which is opened for the first time, and the remaining gas is not directly discharged to the exhaust side, and is sent back to the front of the air supply valve. do.
만약에 밸브가 7개(n=3, p=1)인 경우라면, 급배기 각 3(n)개씩 열리고, 급기 3(n)개와 배기 4(n+1)개가 닫히며, 급기 1개는 퍼지 동작을 하도록 모든 밸브가 순차적으로 교번하여 무한 순환 작동하도록 구비된다. If there are 7 valves (n = 3, p = 1), each 3 (n) of supply / exhaust opens, 3 (n) of supply and 4 (n + 1) of exhaust close, and one supply In order to purge operation, all the valves are provided in order to rotate indefinitely alternately.
이때 퍼지를 담당하는 밸브를 2개 이상으로 하는 것도 가능하지만, 축열 기능의 최대한 발휘를 위해 퍼지를 담당하는 밸브는 그 수를 최소로 하는 것이 바람직하며, 어떤 경우에도 퍼지를 담당하는 급기밸브의 수(p)는 열림 밸브의 수(n) 보다많게 구성해서는 아니된다. At this time, it is possible to have two or more valves in charge of purge, but in order to maximize the heat storage function, it is desirable to minimize the number of valves in charge of purge, and in any case, the number of air supply valves in charge of purge. (p) is not to be greater than the number of open valves (n).
다른 실시예로서, 급기밸브의 작동방식은 상기와 동일하되, 배기밸브의 열림(n)과 닫힘(n+p) 숫자를 반대로 적용할 수도 있다. 즉, 급배기 밸브가 각 5(n=2, P=1)개인 경우를 상정할 배기밸브 3(n+p)개가 열리고, 2(n)개가 닫히는 방식으로 아래와 같은 순서로 작동되도록 할 수 있다.In another embodiment, the operation of the air supply valve is the same as described above, but the number of opening (n) and closing (n + p) of the exhaust valve may be reversed. That is, 3 (n + p) exhaust valves, which are assumed to be 5 (n = 2, P = 1), are opened and 2 (n) are closed to operate in the following order. .
표 2 <배기밸브의 열림 숫자가 닫힘 숫자 보다 적은 경우>
단계 열림(급기/배기) 퍼지(급기) 닫힘(급기/배기)
1 51,52/61,62,63 55 53,54/64,65
2 52,53/62,63,64 51 54,55/65,61
3 53,54/63,64,65 52 55,51/61,62
4 54,55/64,65,61 53 51,52/62,63
5 55,51/65,61,62 54 52,53/63,64
TABLE 2 <When the open valve exhaust number is less than the closed number>
step Open (air supply / exhaust) Fuzzy Air Supply Closed (air supply / exhaust)
One 51,52 / 61,62,63 55 53,54 / 64,65
2 52,53 / 62,63,64 51 54,55 / 65,61
3 53,54 / 63,64,65 52 55,51 / 61,62
4 54,55 / 64,65,61 53 51,52 / 62,63
5 55,51 / 65,61,62 54 52,53 / 63,64
도6은 1단계 밸브 작동에 따라 좌측에 배열된 축열조 구획을 따라 처리용 유해가스가 급기되면서 예열과 해당 축열조의 냉각이 진행되고, 동시적으로 우측에 배열된 축열조 구획을 따라 처리후 가열된 청정가스가 배기되면서 축열조의 열 축적과 배기가스의 냉각이 이루어지는 과정을 나타내고 있다. 6 is a pre-heating and cooling of the corresponding heat storage tank is supplied as the harmful gas for treatment is supplied along the heat storage tank compartment arranged on the left side according to the operation of the first stage valve, and simultaneously cleaned after heating along the heat storage tank compartment arranged on the right side. As the gas is exhausted, heat accumulation in the heat storage tank and cooling of the exhaust gas are shown.
도7은 2단계 밸브 작동에 따라 우측에 배열된 축열조 구획을 따라 처리용 유해가스가 급기되면서 예열과 해당 축열조의 냉각이 진행되고, 동시적으로 좌측에 배열된 축열조 구획을 따라 처리후 가열된 청정가스가 배기되면서 축열조의 열 축적과 배기가스의 냉각이 이루어지는 과정을 나타내고 있다. 도6 및 도7에는 퍼지 밸브(11)가 구비되어 순차적으로 작동하는 급기밸브(51~55)의 퍼지 작동에 따라 해당 급기밸브와 연결된 관내에 잔류한 유해가스를 급기측으로 유도하여 처리되지 않은 오염된 잔류가스가 배기라인을 따라 대기로 배출되지 않도록 한다. 7 is a pre-heating and cooling of the corresponding heat storage tank is supplied as the harmful gas for treatment is supplied along the heat storage tank compartment arranged on the right side according to the operation of the two-stage valve, and simultaneously cleaned after heating along the heat storage tank compartment arranged on the left side. As the gas is exhausted, heat accumulation in the heat storage tank and cooling of the exhaust gas are shown. 6 and 7 are provided with a purge valve 11 in accordance with the purge operation of the air supply valves 51 to 55 in sequence to guide the harmful gas remaining in the pipe connected to the air supply valve to the air supply side untreated pollution Prevent residual gas from being discharged to the atmosphere along the exhaust line.
이후 3~5단계 밸브 작동은 같은 원리에 따라 순환하면서 급기구역과 배기구역을 순차적으로 전환하므로서 5개로 구획된 축열조의 모든 영역이 균일하게 온도를 유지할 수 있도록 작동된다.Afterwards, the three to five stage valves operate according to the same principle to switch the supply and exhaust zones sequentially so that all areas of the five compartments of the heat storage tank are kept at a uniform temperature.
본 발명의 축열식 연소산화장치는 유입덕트(7) 입구측으로 송풍기가 구비되고, 연소실의 고열을 방지하기 위하여 연소실로부터 굴뚝으로 직접 연결된 바이패스관(10)이 더 구비된다.The regenerative combustion oxidation apparatus of the present invention is provided with a blower at the inlet side of the inlet duct (7), and further includes a bypass pipe (10) directly connected to the chimney from the combustion chamber in order to prevent the high temperature of the combustion chamber.
본 발명의 축열식 연소산화장치는 밸브형 급배기 분배실을 구비한 것을 특징으로 하는바, 종래기술에 의해 기 설치된 축열식 연소산화장치에 있어서, 상하부 고정판(41,42)과 수평회전판(50)으로 이루어진 고정통로(40)을 본 발명의 밸브형 급배기 분배실 구조로 대체하는 방법으로 기존 설비를 용이하게 개조하여 사용할 수 있다. 이때 기존의 구획된 축열조와 연소실 등은 그대로 활용할 수 있다.The regenerative combustion oxidizer of the present invention includes a valve type supply / exhaust distribution chamber. In the regenerative combustion oxidizer installed in accordance with the prior art, the upper and lower fixed plates 41 and 42 and the horizontal rotating plate 50 are provided. It is possible to easily modify and use the existing equipment in a way to replace the fixed passage 40 made of the valve-type supply and exhaust distribution structure of the present invention. At this time, the existing compartment heat storage tank and the combustion chamber can be utilized as it is.

Claims (7)

  1. 연소실과 축열조를 구비한 축열식 연소산화장치에 사용되며,Used in regenerative combustion oxidizer with combustion chamber and heat storage tank,
    처리용 유해가스를 공급받아 복수로 구획된 축열조를 거쳐 연소실로 급기하는 급기분배실에 2n+p개의 급기밸브가 구비되고,2n + p air supply valves are provided in the air supply distribution chamber which receives harmful gas for processing and supplies the combustion chamber through a plurality of partitioned heat storage tanks.
    연소실로부터 처리된 청정가스를 복수의 구획된 축열조를 거쳐 공급받아 배기닥트로 배기하는 배기분배실에 같은 수(또는 정수배)의 배기밸브가 구비된 것을 특징으로 하는 축열식 연소산화장치의 급배기용 분배실.Discharge distribution for regenerative combustion oxidizers, characterized in that an exhaust valve having the same number (or an integer multiple) is provided in an exhaust distribution chamber in which clean gas treated from a combustion chamber is supplied through a plurality of partitioned heat storage tanks and exhausted to an exhaust duct. room.
    (여기서 n = 열림 동작하는 급기밸브의 수, p = 퍼지 동작하는 급기밸브의 수)Where n = number of supply valves in open operation, p = number of supply valves in purge operation
  2. 제1항에 있어서, The method of claim 1,
    상기 급기밸브 2n+p개 중 n개 열림, n개 닫힘, p개 퍼지 기능을 담당하도록 순차적으로 교번 동작하며,Of the air supply valve 2n + p n alternately open, n closed, p purge function in order to alternately operate,
    상기 배기밸브 2n+p개 중 n개 또는 n+1개 열림, n+1개 또는 n개 닫힘 기능을 담당하도록 순차적으로 교번 동작하는 것을 특징으로 하는 축열식 연소산화장치의 급배기용 분배실.And n or n + 1 of the exhaust valves 2n + p are alternately operated to sequentially perform the functions of opening, n + 1 or n closing functions of the exhaust valve.
  3. 제2항에 있어서,The method of claim 2,
    상기 p=1인 것을 특징으로 하는 축열식 연소산화장치의 급배기용 분배실.Distributing chamber for supply and exhaust of the regenerative combustion oxidizer, characterized in that p = 1.
  4. 연소실과,Combustion chamber,
    복수의 영역으로 구획된 축열조와,A heat storage tank divided into a plurality of regions,
    급기밸브와 배기밸브를 구비한 급배기 분배실을 포함하되, A supply / exhaust distribution chamber having an air supply valve and an exhaust valve,
    상기 축열조의 구획 수, 급기밸브의 수 및 배기밸브의 수는 각각 2n+p개(또는 그 정수배)이며, The number of compartments of the heat storage tank, the number of air supply valves and the number of exhaust valves are 2n + p (or an integer multiple thereof), respectively.
    상기 급기밸브 2n+p개 중 n개 열림, n개 닫힘 및 p개 퍼지 기능을 담당하도록 순차적으로 교번 동작하는 축열식 연소산화장치.Regenerative combustion oxidizer which is sequentially operated to perform n open, n closed and p purge function of the supply valve 2n + p.
  5. 제4항에 있어서,The method of claim 4, wherein
    상기 급기밸브의 수 만큼 퍼지용 밸브(11)가 더 구비된 것을 특징으로 하는 축열식 연소산화장치.The regenerative combustion oxidation device, characterized in that the purge valve 11 is further provided as many as the air supply valve.
  6. 제4항에 있어서,The method of claim 4, wherein
    상기 축열조를 구획하는 격벽은 방사상 또는 동심원상으로 구획되는 것을 특징으로 하는 축열식 연소산화장치.A partition wall for partitioning the heat storage tank is a regenerative combustion oxidation device, characterized in that partitioned radially or concentrically.
  7. 제4항 내지 제6항 중 어느 하나의 항에 있어서,The method according to any one of claims 4 to 6,
    상기 급기밸브는 개방→퍼지→폐쇄→개방의 순서로 무환 순환하고, 상기 배기밸브는 개방→페쇄→개방 순서로 무환 순환하는 것을 특징으로 하는 축열식 연소산화장치.And the air supply valve is cyclically cycled in the order of opening → purging → closing → opening, and the exhaust valve is cycled in the order of opening → closing → opening.
PCT/KR2011/009030 2010-11-25 2011-11-24 Air intake/exhaust distribution chamber having cyclically operating valves, and regenerative thermal oxidizer comprising same WO2012070892A2 (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106178833A (en) * 2016-08-26 2016-12-07 昆山工统环保科技有限公司 Industrial waste gas zeolite treatment system
WO2017128188A1 (en) * 2016-01-28 2017-08-03 广东环葆嘉节能科技有限公司 Rotary heat accumulating-type waste gas incineration device
CN109386516A (en) * 2017-08-10 2019-02-26 (株)Ksg技术环境 Cylinder driving-type heat-accumulation combustion oxidation treatment device
CN109404938A (en) * 2018-12-11 2019-03-01 恩伟(杭州)环保科技有限公司 A kind of TREATMENT OF VOCs equipment
CN109442440A (en) * 2018-12-03 2019-03-08 汕头东风印刷股份有限公司 A kind of waste gas burning accumulation of heat modularized processing device
CN114060832A (en) * 2021-12-02 2022-02-18 河北天龙环保科技有限公司 Heat accumulating type oxidation system based on alternative use of multiple combustion chambers

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101406023B1 (en) * 2013-06-26 2014-06-11 주식회사 이우이엔티 Regenerative Thermal Oxidizer Having Modularized Heat Storage Chambers Which Are Separated From The Combustion Chamber
KR101714027B1 (en) 2016-07-19 2017-03-09 (주)케이에스지기술환경 Apparatus for regenerative thermal oxidation process with cam operation type
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4650414A (en) * 1985-11-08 1987-03-17 Somerset Technologies, Inc. Regenerative heat exchanger apparatus and method of operating the same
JPH10115412A (en) * 1996-10-09 1998-05-06 Chugai Ro Co Ltd Regenerative deodorizer
JP2003294222A (en) * 2002-04-01 2003-10-15 Chugai Ro Co Ltd Heat-regenerative combustion type deodorization equipment
KR100680028B1 (en) * 2005-08-09 2007-02-08 오석인 Wasteheat recovery system applied for rto

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100472222B1 (en) * 2002-12-10 2005-03-09 유문하 Regenerative thermal oxidizer

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4650414A (en) * 1985-11-08 1987-03-17 Somerset Technologies, Inc. Regenerative heat exchanger apparatus and method of operating the same
JPH10115412A (en) * 1996-10-09 1998-05-06 Chugai Ro Co Ltd Regenerative deodorizer
JP2003294222A (en) * 2002-04-01 2003-10-15 Chugai Ro Co Ltd Heat-regenerative combustion type deodorization equipment
KR100680028B1 (en) * 2005-08-09 2007-02-08 오석인 Wasteheat recovery system applied for rto

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* Cited by examiner, † Cited by third party
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WO2017128188A1 (en) * 2016-01-28 2017-08-03 广东环葆嘉节能科技有限公司 Rotary heat accumulating-type waste gas incineration device
CN106178833A (en) * 2016-08-26 2016-12-07 昆山工统环保科技有限公司 Industrial waste gas zeolite treatment system
CN109386516A (en) * 2017-08-10 2019-02-26 (株)Ksg技术环境 Cylinder driving-type heat-accumulation combustion oxidation treatment device
CN109442440A (en) * 2018-12-03 2019-03-08 汕头东风印刷股份有限公司 A kind of waste gas burning accumulation of heat modularized processing device
CN109404938A (en) * 2018-12-11 2019-03-01 恩伟(杭州)环保科技有限公司 A kind of TREATMENT OF VOCs equipment
CN109404938B (en) * 2018-12-11 2024-04-02 恩伟(杭州)环保科技有限公司 Volatile organic compounds treatment facility
CN114060832A (en) * 2021-12-02 2022-02-18 河北天龙环保科技有限公司 Heat accumulating type oxidation system based on alternative use of multiple combustion chambers

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