TWI482932B - Regenerative combustion exhaust gas purification system and its operation method - Google Patents
Regenerative combustion exhaust gas purification system and its operation method Download PDFInfo
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- TWI482932B TWI482932B TW099124876A TW99124876A TWI482932B TW I482932 B TWI482932 B TW I482932B TW 099124876 A TW099124876 A TW 099124876A TW 99124876 A TW99124876 A TW 99124876A TW I482932 B TWI482932 B TW I482932B
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- 238000002485 combustion reaction Methods 0.000 title claims description 98
- 230000001172 regenerating effect Effects 0.000 title claims description 45
- 238000000746 purification Methods 0.000 title claims description 29
- 238000000034 method Methods 0.000 title claims description 11
- 238000004519 manufacturing process Methods 0.000 claims description 35
- 238000005338 heat storage Methods 0.000 claims description 32
- 230000003068 static effect Effects 0.000 claims description 21
- 230000001105 regulatory effect Effects 0.000 claims description 11
- 238000011144 upstream manufacturing Methods 0.000 claims description 7
- 238000004891 communication Methods 0.000 claims description 4
- 238000007599 discharging Methods 0.000 claims description 4
- 239000007789 gas Substances 0.000 claims 96
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- 239000012855 volatile organic compound Substances 0.000 description 7
- 238000010586 diagram Methods 0.000 description 6
- 238000000354 decomposition reaction Methods 0.000 description 5
- 230000000116 mitigating effect Effects 0.000 description 4
- 238000010790 dilution Methods 0.000 description 3
- 239000012895 dilution Substances 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 230000001276 controlling effect Effects 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/061—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
- F23G7/065—Incinerators 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
- F23G7/066—Incinerators 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
- F23G7/068—Incinerators 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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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2900/00—Special features of, or arrangements for incinerators
- F23G2900/70601—Temporary storage means, e.g. buffers for accumulating fumes or gases, between treatment stages
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- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Incineration Of Waste (AREA)
- Treating Waste Gases (AREA)
Description
本發明,係關於具備蓄熱燃燒式廢氣淨化裝置Regenerative Thermal Oxidizer(以下省略為RTO)與和其運轉時之風量變動對應之靜壓變動緩和用吸引管裝置之蓄熱燃燒式廢氣淨化系統及其運轉方法。The present invention relates to a regenerative combustion type exhaust gas purification system having a regenerative combustion type exhaust gas purifying apparatus Regenerative Thermal Oxidizer (hereinafter abbreviated as RTO) and a static pressure fluctuation mitigation suction tube device corresponding to a change in air volume during operation, and an operation method thereof .
更詳言之,係關於一種蓄熱燃燒式廢氣淨化系統及其運轉方法,其為了避免RTO之氣閘切換時吸引管之靜壓變動影響廢氣發生源之生產設備,藉由在連結於氣體排出生產設備之排氣用送風機與蓄熱燃燒式廢氣淨化裝置RTO用送風機連結之吸引管中設置大氣開放管,而成為大氣緩衝器、亦即吸收或緩和衝擊之緩衝器,可緩和在大氣開放部與吸引管分歧部之一次側(生產設備)之氣閘切換時之靜壓變動之影響,且具備能適應生產設備之排氣風量變動之吸引管裝置。More specifically, it relates to a regenerative combustion type exhaust gas purifying system and a method for operating the same, which is to prevent the static pressure fluctuation of the suction pipe from affecting the production equipment of the exhaust gas generating source during the switching of the air brake of the RTO, by connecting the gas discharge production An exhaust pipe for the exhaust fan of the equipment and a regenerative combustion type exhaust gas purification device RTO are connected to the suction pipe, and an atmospheric open pipe is provided, which serves as an air buffer, that is, a buffer for absorbing or mitigating shock, and can relax the open portion and the suction in the atmosphere. The influence of the static pressure fluctuation at the time of switching the air brake of the primary side (production equipment) of the pipe branching portion, and the suction pipe device that can accommodate the fluctuation of the exhaust air volume of the production equipment.
進而,本發明係關於在設於RTO之氣體供應側之複數個調節式氣閘或設於氣體排出側之複數個調節式氣閘之任一者中,進一步具備即使至少兩個以上之調節式氣閘大致同時開啟亦可防止因RTO導致之壓力損失降低之廢氣供排裝置之蓄熱燃燒式廢氣淨化系統及其運轉方法。Further, the present invention relates to any one of a plurality of adjustable air locks provided on the gas supply side of the RTO or a plurality of adjustable air locks provided on the gas discharge side, and further comprising at least two or more adjustment types The regenerative combustion type exhaust gas purification system of the exhaust gas supply and discharge device and the operation method thereof can be prevented from being simultaneously opened at the same time as the air brake is reduced.
進而,本發明係關於進一步具備用以減低RTO之熱負荷量、防止蓄熱體之損傷之廢氣供排裝置之蓄熱燃燒式廢氣淨化系統。Further, the present invention relates to a regenerative combustion type exhaust gas purification system further comprising an exhaust gas supply and discharge device for reducing the heat load of the RTO and preventing damage of the heat storage body.
當需從廢氣發生源之生產設備排出包含揮發性有機化合物volatile organic compounds(以下省略為VOC)等有害物質之廢氣時,係將廢氣在RTO加熱分解而成為無害後排出至大氣。於生產設備至RTO之廢氣流路,例如有時會為了調整在RTO內之廢氣濃度而配設導入大氣之管。在此種裝置中設置截斷廢氣之導入之氣閘與截斷大氣開放之氣閘例如大氣開放氣閘之方式,亦已為人所知(日本特開2002-61822號公報)。When it is necessary to discharge an exhaust gas containing a harmful substance such as a volatile organic compound (hereinafter referred to as VOC) from a production facility of an exhaust gas generating source, the exhaust gas is decomposed by heating in the RTO to be harmless, and then discharged to the atmosphere. In the exhaust gas flow path from the production equipment to the RTO, for example, a pipe introduced into the atmosphere may be provided in order to adjust the exhaust gas concentration in the RTO. In such a device, a method of providing an air damper for cutting off the exhaust gas and an air damper for opening the atmosphere, such as an open air damper, is also known (JP-A-2002-61822).
然而,習知技術中,如圖5所示,關閉大氣開放氣閘8時RTO(圖中之符號雖係「B」,但以下省略符號)與生產設備A係完全以管連結,而有RTO之入口氣閘9或出口氣閘(未圖示)切換時之靜壓變動經由管傳遞至生產設備之問題。又,如圖6所示,藉由消除大氣開放氣閘並設置大氣開放部管2,成為大氣緩衝器,而能緩和氣閘切換時靜壓變動對生產設備之影響。此情形下,有來自生產設備之廢氣風量會因生產情形變化,而有可能使來自大氣開放管之廢氣洩漏或吸引大氣(空氣)之問題。However, in the conventional technique, as shown in FIG. 5, when the atmosphere is opened, the RTO is closed (the symbol in the figure is "B", but the symbol is omitted below) and the production equipment A is completely connected by a pipe, and there is an RTO. The problem of static pressure fluctuations when the inlet damper 9 or the outlet damper (not shown) is switched to the production equipment via the pipe. Further, as shown in FIG. 6, the atmosphere opening damper is eliminated and the atmosphere opening pipe 2 is provided to form an air damper, and the influence of the static pressure fluctuation on the production equipment during the switching of the air damper can be alleviated. In this case, there is a problem that the amount of exhaust gas from the production equipment may change due to the production situation, and the exhaust gas from the open air of the atmosphere may leak or attract the atmosphere (air).
再者,廢氣之洩漏亦會往大氣排出VOC,而導致問題。Furthermore, the leakage of exhaust gas will also discharge VOCs into the atmosphere, causing problems.
又,大氣被吸引時,廢氣會被稀釋而往RTO導入。由於VOC濃度越高其可燃成分即越多,因此能銷減燃料費用。是以,稀釋廢棄並使VOC濃度降低一事,會導致燃料費用增多。Also, when the atmosphere is attracted, the exhaust gas is diluted and introduced into the RTO. Since the higher the VOC concentration, the more the combustible component is, the fuel cost can be reduced. Therefore, diluting waste and lowering the VOC concentration will result in an increase in fuel costs.
因此,本發明有鑑於上述問題,係提供一種蓄熱燃燒式廢氣淨化系統及其運轉方法,係將用以緩和在RTO之氣閘切換時產生之靜壓變動之大氣開放管,設置於吸引管(將連結於氣體排出生產設備之排氣用送風機與蓄熱燃燒式廢氣淨化裝置RTO用送風機連結)中所設置之大氣開放管與RTO用送風機之間,根據來自連結生產設備與RTO之吸引管之差壓傳動器之靜壓資料,藉由控制氣閘之開度或RTO用送風機運轉反向器之運轉,調整大氣自設置於該吸引管之大氣開放管之流入,藉此即使在來自生產設備之廢氣風量變化亦能以適當之風量運轉RTO。Accordingly, the present invention has been made in view of the above problems, and provides a regenerative combustion type exhaust gas purification system and an operation method thereof, which are provided in an intake pipe for mitigating a static pressure change generated when an RTO air brake is switched. Between the open air pipe and the air blower for RTO installed in the air blower connected to the gas discharge production equipment and the heat storage combustion type exhaust gas purification device RTO, the difference between the suction pipe from the connection production equipment and the RTO The static pressure data of the pressure actuator, by controlling the opening of the air brake or the operation of the inverter operating reverser of the RTO, adjusting the inflow of the atmosphere from the atmospheric open pipe provided in the suction pipe, thereby even from the production equipment The change in exhaust air volume can also operate the RTO with an appropriate air volume.
為解決上述問題,本發明之蓄熱燃燒式廢氣淨化系統及其運轉方法,係將用以緩和在RTO之氣閘切換時產生之靜壓變動之大氣開放管,設置於將連結於氣體排出生產設備之排氣用送風機與蓄熱燃燒式廢氣淨化裝置RTO用送風機連結之吸引管中,且具備控制控制氣閘或吸引用送風機反向器之差壓傳送器,藉此可將大氣開放管之靜壓調整成一定,而可緩和因RTO之入口或出口氣閘導致之靜壓變動對生產設備之影響,且無廢氣排出至大氣並自大氣吸引稀釋空氣之情形亦較少,能對來自生產設備之會變動之排氣風量以適當之吸引風量使RTO運轉。In order to solve the above problems, the regenerative combustion type exhaust gas purification system and the operation method thereof according to the present invention are an atmospheric open pipe for mitigating a static pressure change generated when the RTO air brake is switched, and is installed in a gas discharge production facility. The exhaust fan and the regenerative combustion type exhaust gas purifying device RTO are connected to the suction pipe by a blower, and include a differential pressure transmitter that controls the air brake or the suction fan reverser, thereby allowing static pressure of the atmospheric open pipe. Adjusted to a certain level, and can mitigate the impact of static pressure changes caused by RTO inlet or outlet dampers on production equipment, and no exhaust gas is discharged to the atmosphere and attracts dilution air from the atmosphere, and can be used for production equipment. The amount of exhaust air that will change will cause the RTO to operate with appropriate air volume.
本發明有如下效果,由於係將大氣開放管設置於將連結於氣體排出生產設備之排氣用送風機與蓄熱燃燒式廢氣淨化裝置RTO用送風機連結之吸引管中,且具備控制控制氣閘或吸引用送風機反向器之差壓傳送器,藉此可將大氣開放管之靜壓調整成一定,而可緩和因RTO之入口或出口氣閘導致之靜壓變動對生產設備之影響,且無廢氣排出至大氣並自大氣吸引稀釋空氣之情形亦較少,能對來自生產設備之會變動之排氣風量以適當之吸引風量使RTO運轉。According to the present invention, the atmospheric open pipe is provided in a suction pipe that connects the exhaust air blower connected to the gas discharge production facility and the heat storage combustion type exhaust gas purification device RTO with a blower, and has a control control air lock or suction. The differential pressure transmitter of the blower reverser can adjust the static pressure of the open air tube to a certain level, and can alleviate the influence of static pressure fluctuation caused by the RTO inlet or outlet air brake on the production equipment, and has no exhaust gas. It is also less likely to be discharged to the atmosphere and to draw dilution air from the atmosphere, and the RTO can be operated with an appropriate suction air volume for the variable exhaust air volume from the production equipment.
本申請案,係基於在日本於2009年9月22日提出申請之日本特願2009-218251號,其內容作為本申請案之內容而形成其一部分。The present application is based on Japanese Patent Application No. 2009-218251, filed on Sep. 22, 2009, the content of which is hereby incorporated herein.
又,本發明可藉由如下之詳細說明而能進一步完全理解。然而,詳細說明及特定之實施例僅係本發明之較佳實施形態,僅供說明之目的所記載者。該發明所屬領域具有通常知識者,自可從此詳細說明進行各種變更或改變。Further, the present invention can be further fully understood by the following detailed description. However, the detailed description and specific examples are merely illustrative of the preferred embodiments of the invention The field to which the invention pertains is well known to those skilled in the art, and various changes or modifications can be made herein.
申請人並無將所記載之實施形態之任一者貢獻給大眾之意圖,所揭示之改變、替代案中或許有未於文義上含於申請專利範圍者,然其仍為均等論下之發明之一部分。The applicant does not intend to contribute any of the stated embodiments to the public. The disclosed changes and alternatives may not be included in the scope of the patent application, but it is still the invention of the equalization theory. Part of it.
本說明書或申請專利範圍之記載中,名詞及相同之指示語之使用只要無特別指示,或依其文脈無法明確否定者,均應解釋為包含單數及複數兩者。本說明書所提供之任一例示或例示性之用語(例如「等」)之使用,亦不過係為使說明易於理解之目的,只要未特別記載於申請專利範圍,則非對本發明之範圍施以限制。In the description of the specification or the scope of the patent application, the use of the noun and the same referent should be construed as including the singular and plural, unless otherwise specified. The use of any exemplification or exemplification of the present invention (such as "the", etc.) is used for the purpose of making the description easy to understand, and the scope of the present invention is not to be construed as being limit.
以下,根據附圖說明本發明之實施形態。此外,對同一或類似之要素使用同一符號,省略重複之說明。本發明之一實施形態之RTO與自生產設備對RTO供應廢氣之吸引管裝置之構成,如圖1所示從兩處以上進行吸引之情形下,係於各生產設備A1,A2之排氣用送風機1,21之二次排氣側設置常時對大氣開放之大氣開放管2,22。又,於大氣開放管2,22與RTO用送風機4之間依來自各裝置之排氣線路設置控制氣閘5,25(開度可調整氣閘)。Hereinafter, embodiments of the present invention will be described with reference to the drawings. In addition, the same reference numerals are used for the same or similar elements, and the repeated description is omitted. In the case where the RTO of the embodiment of the present invention and the suction pipe device for supplying the exhaust gas to the RTO from the production equipment are sucked from two or more places as shown in Fig. 1, the exhaust gas is used for the exhaust of each of the production facilities A1 and A2. The secondary exhaust side of the blowers 1, 21 is provided with atmospheric open pipes 2, 22 which are normally open to the atmosphere. Further, the air locks 5, 25 (opening adjustable dampers) are provided between the atmosphere open pipes 2, 22 and the RTO blower 4 in accordance with the exhaust lines from the respective devices.
在來自生產設備A1,A2之最大排氣風量時,係使控制氣閘5,25全開而進行整體之吸引風量之調整,藉此使吸引管之壓力損失成為最小。又,以差壓傳送器3,23測定各線路之大氣開放管2,22之靜壓,而以控制氣閘5,25自動調整成其靜壓值相對廢氣之風量變化為-0.05~±0.00kPa(設定值)。In the case of the maximum exhaust air volume from the production equipment A1, A2, the control air locks 5, 25 are fully opened to adjust the overall suction air volume, thereby minimizing the pressure loss of the suction pipe. Further, the differential pressure transmitters 3, 23 are used to measure the static pressure of the atmospheric open tubes 2, 22 of each line, and the control air locks 5, 25 are automatically adjusted to have a static pressure value of -0.05 to ±0.00 with respect to the exhaust gas. kPa (set value).
藉由以上,可緩和因RTO之氣閘導致之靜壓變動對生產設備之影響。By the above, the influence of the static pressure fluctuation caused by the RTO air brake on the production equipment can be alleviated.
為了消除來自大氣開放管2,22之洩漏、吸引,係將吸引管內調整成負壓。藉此能防止廢氣放出至大氣。當將吸引管內控制成負壓,由於係從大氣開放部導入外部氣體,因此雖產生廢氣濃度降低之情形,但其影響僅為些微,與廢氣放出至大氣之問題相較,可知些微之稀釋係在容許範圍內。In order to eliminate leakage and attraction from the open tubes 2, 22, the suction tube is adjusted to a negative pressure. Thereby, the exhaust gas can be prevented from being released to the atmosphere. When the suction pipe is controlled to a negative pressure, since the external gas is introduced from the open portion of the atmosphere, although the concentration of the exhaust gas is lowered, the influence is only slight, and the dilution is slightly compared with the problem that the exhaust gas is released to the atmosphere. It is within the allowable range.
又,本發明之另一實施形態之構成,係如圖2所示,在從一處之生產設備A進行吸引之情形下,係於排氣用送風機1之二次排氣側設置常時對大氣開放之大氣開放管2。Further, in the configuration of the other embodiment of the present invention, as shown in Fig. 2, when suction is performed from the production facility A, the secondary exhaust side of the exhaust fan 1 is always placed at the atmosphere. Open atmosphere open tube 2.
以反向器6將RTO用送風機4之頻率自動調整成其靜壓值相對來自生產設備A之廢氣之風量變化為-0.05~±0.00kPa(設定值)。藉此,可在不需控制氣閘之狀態下進行與以圖1說明之實施形態相同之控制。The frequency of the RTO blower 4 is automatically adjusted by the inverter 6 to a static pressure value of -0.05 to ±0.00 kPa (set value) with respect to the air volume of the exhaust gas from the production equipment A. Thereby, the same control as that of the embodiment illustrated in Fig. 1 can be performed without controlling the air lock.
其次,說明將吸引管裝置與RTO連通並排出來自RTO之已處理廢氣之廢氣供排裝置。具有複數個蓄熱室且對含有揮發性有機化合物等之可燃性有害成分之廢氣進行燃燒處理之RTO中,於RTO之廢氣供應側(對RTO之入口)與來自RTO之排出側(來自RTO之出口)分別設置具有複數個調節式氣閘之廢氣供排裝置,藉由開閉調節式氣閘來進行前述廢氣之供排。Next, an exhaust gas supply and discharge device that connects the suction pipe device to the RTO and discharges the treated exhaust gas from the RTO will be described. RTO having a plurality of regenerators for burning exhaust gas containing flammable harmful components such as volatile organic compounds, on the exhaust gas supply side of RTO (input to RTO) and the discharge side from RTO (from RTO outlet) The exhaust gas supply and discharge device having a plurality of regulated air locks is separately provided, and the exhaust gas is supplied and discharged by opening and closing the adjustable air lock.
然而,上述構成之習知廢氣供排裝置中,供應側之調節式氣閘與排出側之調節式氣閘係同時有兩個以上成為「開啟」之狀態(雖僅為一瞬間),伴隨與此使RTO導致之壓力損失降低而使供應至RTO之廢氣量增大,其結果,有可能使蓄熱燃燒式廢氣淨化系統(包含RTO及對RTO之廢氣供應用及來自RTO之廢氣排出用管等)產生靜壓變動。此靜壓變動有可能對生產設備帶來影響。However, in the conventional exhaust gas supply and discharge device of the above configuration, the two types of the damper type on the supply side and the damper type on the discharge side are simultaneously "opened" (although only for a moment), accompanied by This reduces the pressure loss caused by the RTO and increases the amount of exhaust gas supplied to the RTO. As a result, the regenerative combustion type exhaust gas purification system (including the RTO, the exhaust gas supply to the RTO, and the exhaust gas discharge pipe from the RTO) may be used. ) Static pressure changes occur. This static pressure change may have an impact on the production equipment.
因此,如圖3所示,於供排手段32設置廢氣回歸手段33。供排手段32,藉由使分別設於RTO之廢氣供應側及排出側之複數個調節式氣閘37,38,39,40連動開閉,來對RTO進行前述廢氣之供排。廢氣回歸手段33,在藉由使複數個調節式氣閘37,38,39,40中至少兩個以上之調節式氣閘大致同時開啟使RTO導致之壓力損失降低時,將從前述排出側調節式氣閘39,40排出之已處理廢氣一部分,送入至配設在RTO之廢氣供應側之RTO用送風機4之吸引側。Therefore, as shown in FIG. 3, the exhaust gas return means 33 is provided in the supply and discharge means 32. The supply and discharge means 32 intermittently opens and closes a plurality of adjustable air locks 37, 38, 39, 40 provided on the exhaust gas supply side and the discharge side of the RTO, respectively, to supply and discharge the exhaust gas to the RTO. The exhaust gas returning means 33 adjusts from the discharge side by reducing the pressure loss caused by the RTO by causing at least two of the plurality of adjustable air brakes 37, 38, 39, 40 to open at substantially the same time. A part of the treated exhaust gas discharged from the air brakes 39, 40 is sent to the suction side of the RTO blower 4 disposed on the exhaust gas supply side of the RTO.
接著,在前述廢氣之供排手段32中,於與產生廢氣之廢氣產生裝置A1,A2(參照圖1)連通之吸引管34前端連接有RTO用送風機4之吸引口,於RTO用送風機4之放出口連接有未處理廢氣供應管36之一端。未處理廢氣供應管36之另一端分別經由兩個調節式氣閘37,38分別連接於RTO之廢氣供應口,於RTO之已處理廢氣排出口經由兩個調節式氣閘39,40及已處理廢氣排氣管41連接有排氣管42。又,於前述吸引管34安裝壓力傳送器43,且於前述未處理廢氣供應管36安裝具備差壓傳送器44之孔口流量計51,安裝於前述RTO用送風機4之電動機45之反向器46、前述壓力傳送器43及差壓傳送器44係經由控制器47彼此電氣連接。Next, in the exhaust gas supply and discharge means 32, the suction port of the RTO blower 4 is connected to the front end of the suction pipe 34 that communicates with the exhaust gas generating devices A1, A2 (see Fig. 1), and the RTO blower 4 One end of the untreated exhaust gas supply pipe 36 is connected to the discharge port. The other end of the untreated exhaust gas supply pipe 36 is respectively connected to the exhaust gas supply port of the RTO via two regulating air locks 37, 38, and the treated exhaust gas discharge port of the RTO is passed through two adjustable air locks 39, 40 and processed. An exhaust pipe 42 is connected to the exhaust gas exhaust pipe 41. Further, the pressure transmitter 43 is attached to the suction pipe 34, and the orifice flowmeter 51 including the differential pressure transmitter 44 is attached to the untreated exhaust gas supply pipe 36, and the reverser of the motor 45 attached to the RTO blower 4 is attached. 46. The pressure transmitter 43 and the differential pressure transmitter 44 are electrically connected to each other via a controller 47.
又,前述廢氣回歸手段33中,附設有流量調整氣閘48之管49連通連接於吸引管34與已處理廢氣排氣管41間,流量調整氣閘48之定位器50電氣連接於前述控制器47。Further, in the exhaust gas returning means 33, a pipe 49 to which the flow rate adjusting damper 48 is attached is connected between the suction pipe 34 and the treated exhaust gas exhaust pipe 41, and the positioner 50 of the flow rate adjusting damper 48 is electrically connected to the controller. 47.
如上構成之裝置,係將未處理之廢氣誘導至吸引管34,且藉由RTO用送風機4加壓而送入至未處理廢氣供應管36,使複數個調節式氣閘37~40連動開閉,而對RTO進行廢氣之供排之既定處理。接著,根據藉由壓力傳送器43測定之吸引管34內之壓力及藉由差壓傳送器44測定之孔口流量計51之差壓,透過控制器47調整流量調整氣閘48之開度。In the apparatus configured as described above, the untreated exhaust gas is induced to the suction pipe 34, and is pressurized by the RTO blower 4 to be sent to the untreated exhaust gas supply pipe 36, so that the plurality of regulated air brakes 37 to 40 are interlocked to open and close. For the RTO, the exhaust gas supply and discharge are scheduled. Next, the opening of the flow rate adjusting damper 48 is adjusted by the controller 47 based on the pressure in the suction pipe 34 measured by the pressure transmitter 43 and the differential pressure of the orifice flow meter 51 measured by the differential pressure transmitter 44.
如上所述在處理廢氣之途中,調節式氣閘37~40中至少兩個以上之調節式氣閘係同時成為「開啟」之狀態,伴隨於此使RTO導致之壓力損失降低而供應至RTO之廢氣量即將增大時,係根據壓力傳送器43及差壓傳送器44之測定結果,藉由控制器47控制流量調整氣閘48,使從調節式氣閘39,40排出之已處理廢氣經由管49及流量調整氣閘48返回至吸引管34。藉此,能防止因調節式氣閘之同時「開啟」導致對RTO之廢氣供應量增大。As described above, in the process of treating the exhaust gas, at least two of the regulated air brakes of the adjustable air brakes 37 to 40 are simultaneously "opened", and the pressure loss caused by the RTO is lowered to be supplied to the RTO. When the amount of exhaust gas is about to increase, the flow rate adjustment damper 48 is controlled by the controller 47 according to the measurement results of the pressure transmitter 43 and the differential pressure transmitter 44, so that the exhausted exhaust gas discharged from the damper dampers 39, 40 is passed through The tube 49 and the flow regulating damper 48 are returned to the suction tube 34. Thereby, it is possible to prevent an increase in the exhaust gas supply to the RTO due to the "on" of the damper at the same time.
又,習知RTO中,廢氣在通過蓄熱室後,係在保持於分解對象成分所需之溫度(較對象成分燃點溫度高出200~300℃之溫度)之燃燒室內進行高溫燃燒分解處理。此時,當廢氣中之對象成分濃度變高時,成分本身則會發揮燃料之效果,在燃燒室或蓄熱室燃燒後之結果,使燃燒室內成為前述保持溫度以上之溫度。是以,恐有在廢氣之預備加熱步驟(從裝置入口至燃燒室)及成分分解後之熱回收步驟(從燃燒室至裝置出口)中施加於蓄熱體之熱負荷量變大之情事。Further, in the conventional RTO, after passing through the regenerator, the exhaust gas is subjected to a high-temperature combustion decomposition treatment in a combustion chamber which is maintained at a temperature required for the component to be decomposed (a temperature higher than a target component ignition temperature by 200 to 300 ° C). At this time, when the concentration of the target component in the exhaust gas becomes high, the component itself exerts the effect of the fuel, and as a result of combustion in the combustion chamber or the regenerator, the inside of the combustion chamber becomes a temperature equal to or higher than the above-described holding temperature. Therefore, there is a fear that the amount of heat applied to the heat storage body in the heat recovery step of the exhaust gas (from the inlet of the apparatus to the combustion chamber) and the heat recovery step after the decomposition of the components (from the combustion chamber to the outlet of the apparatus) becomes large.
例如於表1顯示,在處理風量:100m3/min(0℃、101.3kPa時)、甲苯濃度:0,500,1500,3000,5000ppm(甲苯之自然燃燒開始濃度:500ppm)、裝置入口氣體溫度:20℃之情形下,算出燃燒室內溫度及RTO出口氣體溫度之結果。根據表1可知,甲苯濃度越高則越多產生燃燒熱,使燃燒室內溫度及RTO出口氣體溫度變高。For example, in Table 1, the air volume is treated: 100 m3/min (0 ° C, 101.3 kPa), toluene concentration: 0,500, 1500, 3000, 5000 ppm (natural combustion start concentration of toluene: 500 ppm), device inlet gas temperature: 20 ° C In the case, the temperature in the combustion chamber and the temperature of the RTO outlet gas are calculated. As is clear from Table 1, the higher the toluene concentration, the more heat of combustion is generated, and the temperature in the combustion chamber and the temperature of the RTO outlet gas become higher.
蓄熱體若暴露於過度之高溫度中,即會如上所述使施加於蓄熱體之熱負荷量增大,而有可能產生蓄熱體之裂痕或龜裂等。When the heat storage body is exposed to an excessively high temperature, the amount of heat load applied to the heat storage body is increased as described above, and cracks or cracks of the heat storage body may occur.
RTO及廢氣供排裝置之另一實施形態顯示於圖4。圖4所示之RTO,係於內部分別配設蓄熱體61a,62a,63a,且具備並排構成之蓄熱室61,62,63,蓄熱室61,62,63之上部連通連接於共通之燃燒室64。又,前述蓄熱室61,62,63中之蓄熱體61a,62a,63a下方與各入口(供應側)氣閘65,66,67及各出口(排出側)氣閘68,69,70係分別連通連接。進而,前述各入口氣閘65,66,67與未處理廢氣供應管36連通連接,前述各出口氣閘68,69,70與已處理廢氣排氣管41連通連接。Another embodiment of the RTO and the exhaust gas supply and discharge device is shown in FIG. The RTO shown in FIG. 4 is internally provided with heat storage bodies 61a, 62a, 63a, and has regenerative chambers 61, 62, 63 arranged side by side, and the upper portions of the regenerators 61, 62, 63 are connected to the common combustion chamber. 64. Further, in the heat storage chambers 61, 62, 63, the heat storage bodies 61a, 62a, 63a below the respective inlet (supply side) air locks 65, 66, 67 and the respective outlet (discharge side) air locks 68, 69, 70 are respectively Connected connections. Further, each of the inlet dampers 65, 66, 67 is in communication with the untreated exhaust gas supply pipe 36, and the respective outlet dampers 68, 69, 70 are connected in communication with the treated exhaust gas exhaust pipe 41.
又,於前述未處理廢氣供應管36之前述入口氣閘65上游位置連通連接有新鮮空氣導入氣閘71,且將該未處理廢氣供應管36中之前述入口氣閘65之上游位置與前述燃燒室64經由冷旁路氣閘72連通連接。此外,圖4中,前述冷旁路氣閘72之連接位置,雖在前述未處理廢氣供應管36中之前述入口氣閘65之連接位置與新鮮空氣導入氣閘71之連接位置之間,但該冷旁路氣閘72之連接位置不限定於此,亦可較新鮮空氣導入氣閘71之連接位置更上游側。Further, a fresh air introduction damper 71 is continuously connected to the upstream of the inlet damper 65 of the untreated exhaust gas supply pipe 36, and the upstream position of the inlet damper 65 in the untreated exhaust gas supply pipe 36 is compared with the foregoing combustion. Chamber 64 is connected in communication via a cold bypass damper 72. In addition, in FIG. 4, the connection position of the cold bypass damper 72 is between the connection position of the inlet damper 65 in the untreated exhaust gas supply pipe 36 and the connection position of the fresh air introduction damper 71, but The connection position of the cold bypass damper 72 is not limited thereto, and may be further upstream than the connection position of the fresh air introduction damper 71.
此處,本發明中之新鮮氣體,係指例如室外或工廠內之大氣,亦包含通過粗塵過濾器等之前述大氣。Here, the fresh gas in the present invention means, for example, an atmosphere in an outdoor or factory, and also includes the aforementioned atmosphere passing through a coarse dust filter or the like.
又,本發明中之冷旁路氣閘,係指用以使廢氣不通過蓄熱室而直接導入燃燒室之氣閘。此外,圖4所示之任一氣閘亦可係調節式氣閘。Further, the cold bypass air brake in the present invention means an air lock for directly introducing the exhaust gas into the combustion chamber without passing through the regenerator. In addition, any of the air locks shown in FIG. 4 may also be an adjustable air lock.
再者,前述已處理廢氣排氣管41中之前述出口氣閘70之下游位置與前述燃燒室64係經由熱旁路氣閘73連通連接。此外,於前述燃燒室64內,設置有用以保持該燃燒室64之室內溫度而使用之作為燃燒室內溫度保持手段之燃燒器74。Further, a position downstream of the outlet damper 70 in the exhaust gas exhaust pipe 41 is connected to the combustion chamber 64 via a heat bypass damper 73. Further, in the combustion chamber 64, a burner 74 which is used as a temperature holding means in the combustion chamber for holding the indoor temperature of the combustion chamber 64 is provided.
本發明中之熱旁路氣閘,係指用以將經燃燒分解之已處理廢氣從燃燒室內排出,不蓄熱於蓄熱體而將剩餘熱量廢棄之氣閘。The heat bypass damper in the present invention refers to an air damper for discharging the treated exhaust gas which has been burned and decomposed from the combustion chamber, and not storing heat in the heat storage body to discard the remaining heat.
說明如上述構成之蓄熱燃燒式廢氣淨化系統之作動。首先,藉由燃燒器74將燃燒室64之室內溫度保持於分解對象成分所需之溫度(較對象成分燃點溫度高出200~300℃之溫度),且先使新鮮空氣導入氣閘71、冷旁路氣閘72及熱旁路氣閘73均成為關閉狀態。The operation of the regenerative combustion type exhaust gas purifying system constructed as described above will be described. First, the indoor temperature of the combustion chamber 64 is maintained at a temperature required for the decomposition target component by the burner 74 (a temperature higher than the ignition temperature of the target component by 200 to 300 ° C), and fresh air is first introduced into the air lock 71 and cooled. Both the bypass damper 72 and the hot bypass damper 73 are in a closed state.
在此狀態下,從未處理廢氣供應管36供應之含有揮發性有機化合物等成分之廢氣,係在「入口氣閘65開啟、出口氣閘69開啟、其他入口氣閘66,67及出口氣閘68,70關閉」之狀態下通過入口氣閘65而導入至蓄熱室61,通過蓄熱室61時被預備加熱而在燃燒室64被燃燒分解。接著,藉由該燃燒分解而淨化之廢氣,在通過蓄熱室62之蓄熱體62a時進行熱交換後,通過出口氣閘69從已處理廢氣排氣管41排出。In this state, the exhaust gas containing components such as volatile organic compounds supplied from the untreated exhaust gas supply pipe 36 is "opening of the inlet damper 65, opening of the outlet damper 69, other inlet dampers 66, 67 and the outlet damper. In the state where 68, 70 is closed, the inlet air lock 65 is introduced into the regenerator 61, and when it passes through the regenerator 61, it is preheated and burned and decomposed in the combustion chamber 64. Then, the exhaust gas purified by the combustion decomposition is subjected to heat exchange while passing through the heat storage body 62a of the regenerator 62, and then discharged from the treated exhaust gas exhaust pipe 41 through the outlet damper 69.
其次,在經過既定時間後,切換成「入口氣閘66開啟、出口氣閘70開啟、其他入口氣閘65,67及出口氣閘68,69關閉」之狀態。在此狀態下,前述廢氣係通過入口氣閘66及出口氣閘70,經與上述相同之處理後被排出。Next, after a predetermined period of time, the state is switched to "the inlet damper 66 is opened, the outlet damper 70 is opened, the other inlet dampers 65, 67, and the outlet damper 68, 69 are closed". In this state, the exhaust gas passes through the inlet damper 66 and the outlet damper 70, and is discharged after the same treatment as described above.
進一步地,在經過既定時間後,切換成「入口氣閘67開啟、出口氣閘68開啟、其他入口氣閘65,66及出口氣閘69,70關閉」之狀態。在此狀態下,前述廢氣係通過入口氣閘67及出口氣閘68,經與上述相同之處理後被排出。其次,在經過既定時間後,切換成最初之「入口氣閘65開啟、出口氣閘69開啟、其他入口氣閘66,67及出口氣閘68,70關閉」之狀態,並反覆上述作動。Further, after a predetermined period of time, the state is switched to "the inlet damper 67 is opened, the outlet damper 68 is opened, the other inlet dampers 65, 66, and the outlet damper 69, 70 are closed". In this state, the exhaust gas passes through the inlet damper 67 and the outlet damper 68, and is discharged after the same treatment as described above. Next, after a predetermined period of time, the state is switched to the state of "the inlet damper 65 is opened, the outlet damper 69 is opened, the other inlet dampers 66, 67, and the outlet damper 68, 70 are closed", and the above operation is repeated.
此外,在反覆上述作動中,當前述廢氣中之成分濃度或對象成分之溫度上升度較高時,可預測燃燒室64內之溫度變得較保持溫度(較對象成分燃點溫度高出200~300℃之溫度)高。此情形下,在裝置之運作中,首先停止前述燃燒器74。接著,開啟熱旁路氣閘73,將已淨化之廢氣一部分從燃燒室64內排出,並在不蓄熱於蓄熱體61a,62a,63a之狀態下將剩餘熱量廢棄,且開啟新鮮空氣導入氣閘71,以新鮮氣體稀釋所供應之廢氣中之成分濃度,使燃燒室64內之溫度不過於上升。通常,以上述方式減輕施加於蓄熱體61a,62a,63a之熱負荷量。Further, in the above-described operation, when the concentration of the component in the exhaust gas or the temperature rise of the target component is high, it is predicted that the temperature in the combustion chamber 64 becomes higher than the holding temperature (200 to 300 higher than the ignition temperature of the target component). The temperature of °C is high. In this case, in the operation of the apparatus, the aforementioned burner 74 is first stopped. Next, the hot bypass damper 73 is turned on, a part of the purified exhaust gas is discharged from the combustion chamber 64, and the remaining heat is discarded without accumulating heat in the heat storage bodies 61a, 62a, 63a, and the fresh air is introduced into the air lock. 71. The concentration of the components in the supplied exhaust gas is diluted with fresh gas so that the temperature in the combustion chamber 64 does not rise. Usually, the amount of heat applied to the heat storage bodies 61a, 62a, 63a is reduced in the above manner.
然而,當前述廢氣中之成分濃度或對象成分之溫度上升度極高時,有時即使如上述般停止前述燃燒器74,開啟熱旁路氣閘73及新鮮空氣導入氣閘71,燃燒室64內之溫度亦會超過蓄熱體61a,62a,63a之耐熱溫度。在此情形下,於裝置之運作中前述燃燒器74停止之狀態下,開啟冷旁路氣閘72,使廢氣一部分不通過蓄熱室61,62,63而直接導入至燃燒室64進行燃燒分解,且開啟熱旁路氣閘73,將已淨化之廢氣一部分從燃燒室64內排出以廢棄剩餘熱量。如上述般,藉由減少廢氣在蓄熱室61,62,63內之燃燒且減少已淨化之廢氣在蓄熱室61,62,63之熱交換,而能更加減輕施加於蓄熱體61a,62a,63a之熱負荷。However, when the concentration of the component in the exhaust gas or the temperature rise of the target component is extremely high, sometimes the burner 74 is stopped as described above, the hot bypass damper 73 and the fresh air introduction damper 71 are turned on, and the combustion chamber 64 The temperature inside also exceeds the heat-resistant temperature of the heat storage bodies 61a, 62a, 63a. In this case, in the state in which the burner 74 is stopped during the operation of the apparatus, the cold bypass damper 72 is opened, so that a part of the exhaust gas is directly introduced into the combustion chamber 64 without being passed through the regenerators 61, 62, 63 for combustion decomposition. The hot bypass damper 73 is turned on, and a portion of the purified exhaust gas is exhausted from the combustion chamber 64 to discard the remaining heat. As described above, by reducing the combustion of the exhaust gas in the regenerators 61, 62, 63 and reducing the heat exchange of the purified exhaust gas in the regenerators 61, 62, 63, it is possible to more reduce the application to the regenerators 61a, 62a, 63a. The heat load.
此外,新鮮空氣導入氣閘71原則上係關閉。其係為了避免廢氣處理量降低。不過,在使燃燒室64內之溫度更加下降一事有優先必要時,亦可開啟新鮮空氣導入氣閘71,而以新鮮氣體稀釋所供應之廢氣中之成分濃度。又,前述廢氣對燃燒室64之直接導入,亦可非為廢氣之一部分而為廢氣全量。此情形下,入口氣閘65,66,67均為關閉。Furthermore, the fresh air introduction damper 71 is in principle closed. It is to avoid a reduction in the amount of exhaust gas treatment. However, when it is necessary to lower the temperature in the combustion chamber 64 more preferably, the fresh air introduction damper 71 may be turned on, and the concentration of the components in the supplied exhaust gas may be diluted with fresh gas. Further, the direct introduction of the exhaust gas to the combustion chamber 64 may be a part of the exhaust gas and may be the total amount of the exhaust gas. In this case, the inlet dampers 65, 66, 67 are all closed.
此外,本發明之實施形態中,雖係藉由熱旁路氣閘73之開啟,而從燃燒室64內排出已淨化之廢氣之一部分,但亦可非為已淨化之廢氣之一部分而為全量。此情形下,出口氣閘68,69,70均為關閉。Further, in the embodiment of the present invention, a part of the purified exhaust gas is discharged from the combustion chamber 64 by the opening of the hot bypass damper 73, but it may not be a part of the purified exhaust gas. . In this case, the outlet dampers 68, 69, 70 are all closed.
1,21...排氣用送風機1,21. . . Exhaust blower
2,22...大氣開放管2,22. . . Atmospheric open tube
3,23...差壓傳送器3,23. . . Differential pressure transmitter
4...RTO用送風機4. . . RTO blower
5,25...控制氣閘5,25. . . Control air lock
6...反向器6. . . Inverter
32...供排手段32. . . Supply and discharge means
33...廢氣回歸手段33. . . Exhaust gas regression
34...吸引管34. . . Suction tube
36...未處理廢氣供應管36. . . Untreated exhaust gas supply pipe
37,38,39,40...調節式氣閘37,38,39,40. . . Adjustable air lock
41...已處理廢氣排氣管41. . . Exhaust exhaust pipe
42...排氣管42. . . exhaust pipe
43...壓力傳送器43. . . Pressure transmitter
44...差壓傳送器44. . . Differential pressure transmitter
45...電動機45. . . electric motor
46...反向器46. . . Inverter
47...控制器47. . . Controller
48...流量調整氣閘48. . . Flow regulation air lock
49...管49. . . tube
50...定位器50. . . Locator
51...孔口流量計51. . . Orifice flowmeter
61,62,63...蓄熱室61,62,63. . . Regenerator
61a,62a,63a...蓄熱體61a, 62a, 63a. . . Heat accumulator
64...燃燒室64. . . Combustion chamber
65,66,67...氣閘65,66,67. . . Air brake
68,69,70...出口氣閘68,69,70. . . Export air lock
71...新鮮空氣導入氣閘71. . . Fresh air introduction air lock
72...冷旁路氣閘72. . . Cold bypass air lock
73...熱旁路氣閘73. . . Thermal bypass air brake
74...燃燒器74. . . burner
A,A1,A2...生產設備A, A1, A2. . . Production equipment
B...RTOB. . . RTO
圖1係本發明之蓄熱燃燒式廢氣淨化系統之吸引線路為兩處以上時之方塊圖。Fig. 1 is a block diagram showing a case where the attraction line of the regenerative combustion type exhaust gas purification system of the present invention is two or more.
圖2係本發明之蓄熱燃燒式廢氣淨化系統之吸引線路為一處時之方塊圖。Fig. 2 is a block diagram showing the attraction line of the regenerative combustion type exhaust gas purifying system of the present invention in one place.
圖3係顯示本發明之RTO與廢氣供排裝置之方塊圖。Figure 3 is a block diagram showing the RTO of the present invention and an exhaust gas supply and discharge device.
圖4係顯示本發明之RTO與廢氣供排裝置之實施形態之廢氣處理裝置之概要構成圖。Fig. 4 is a schematic block diagram showing an exhaust gas treating apparatus of an embodiment of the RTO and the exhaust gas supply and discharge device of the present invention.
圖5係具備大氣開放氣閘之習知方式之蓄熱燃燒式廢氣淨化系統之方塊圖(其1)。Fig. 5 is a block diagram (1) of a conventional heat storage combustion type exhaust gas purification system having an open air damper.
圖6係具備大氣開放氣閘之習知方式之蓄熱燃燒式廢氣淨化系統之方塊圖(其2)。Fig. 6 is a block diagram (2) of a conventional heat storage combustion type exhaust gas purification system having an open air damper.
1,21...排氣用送風機1,21. . . Exhaust blower
2,22...大氣開放管2,22. . . Atmospheric open tube
3,23...差壓傳送器3,23. . . Differential pressure transmitter
4...RTO用送風機4. . . RTO blower
5,25...控制氣閘5,25. . . Control air lock
A1,A2...生產設備A1, A2. . . Production equipment
B...RTOB. . . RTO
Claims (7)
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| JP2009218251 | 2009-09-22 |
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| JP (1) | JP5344043B2 (en) |
| CN (1) | CN102498345B (en) |
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| CN102498345A (en) | 2012-06-13 |
| WO2011036940A1 (en) | 2011-03-31 |
| JP5344043B2 (en) | 2013-11-20 |
| JPWO2011036940A1 (en) | 2013-02-14 |
| CN102498345B (en) | 2014-06-11 |
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