TW202217195A - Energy-saving single runner hot-side bypass temperature control system and method which can prevent the direct-fired incinerator (TO) from overheating due to too high furnace temperature when the organic waste gas is treated - Google Patents

Energy-saving single runner hot-side bypass temperature control system and method which can prevent the direct-fired incinerator (TO) from overheating due to too high furnace temperature when the organic waste gas is treated Download PDF

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TW202217195A
TW202217195A TW109136204A TW109136204A TW202217195A TW 202217195 A TW202217195 A TW 202217195A TW 109136204 A TW109136204 A TW 109136204A TW 109136204 A TW109136204 A TW 109136204A TW 202217195 A TW202217195 A TW 202217195A
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pipeline
hot
gas
heat exchanger
adsorption
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TW109136204A
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TWI826737B (en
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鄭石治
林國源
扶亞民
陳宗賢
劉邦昱
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華懋科技股份有限公司
大陸商上海華懋環保節能設備有限公司
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Priority to TW109136204A priority Critical patent/TWI826737B/en
Priority to CN202011419941.0A priority patent/CN114377516A/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/06Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with moving adsorbents, e.g. rotating beds
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44Details; Accessories
    • F23G5/46Recuperation of heat
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/50Control or safety arrangements
    • 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/70Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/708Volatile organic compounds V.O.C.'s

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)

Abstract

The present invention relates to an energy-saving single runner hot-side bypass temperature control system and method thereof, mainly used in an organic waste gas treatment system. The energy-saving single runner hot-side bypass temperature control system includes a direct-fired incinerator (TO), a first heat exchanger, a second heat exchanger, a first cold-side delivery pipe, an adsorption runner and a chimney. A hot-side forcible discharge pipe is disposed in the furnace of the direct-fired incinerator (TO). Further, the other end of the hot-side forcible discharge pipe is connected with the connection between the second hot-side pipe of the second heat exchanger and the first hot-side pipe of the first heat exchanger, or connected to any place of the outlets of the direct-fired incinerator (TO). Thus, when the concentration of volatile organic compounds (VOCs) becomes high, the air volume of the furnace of the direct-fired incinerator (TO) can be adjusted through the hot-side forcible discharge pipe so as to have the effect of adjusting the amount or concentration of heat recovery. When the organic waste gas is treated, it can prevent the direct-fired incinerator (TO) from overheating due to too high furnace temperature and even leading to shutdown. The direct-fired incinerator includes a burner head and a furnace. The burner head and the furnace are connected with each other. The direct-fired incinerator has an inlet and an outlet. The inlet is disposed at the burner head and the outlet is disposed at the furnace. The first heat exchanger is disposed in the direct-fired incinerator and has a first cold-side pipe and a first hot-side pipe. The second heat exchanger is disposed in the direct-fired incinerator and has a second cold-side pipe and a second hot-side pipe. One end of the first cold-side delivery pipe is connected to the other end of the first cold-side pipe, and the other end of the first cold-side delivery pipe is connected to the inlet of the direct-fired incinerator.

Description

節能型單轉輪熱側旁通過溫控制系統及其方法 Energy-saving single runner hot side bypass temperature control system and method

本發明係有關於一種節能型單轉輪熱側旁通過溫控制系統及其方法,尤指一種當揮發性有機化合物(VOCs)濃度變高時,能具有調節熱回收量或濃度之效能,使有機廢氣在處理時,能防止直燃式焚燒爐(TO)不會因爐溫太高而發生過溫之現象,甚至導致停機之情形發生,而適用於半導體產業、光電產業或化學相關產業的有機廢氣處理系統或類似設備。 The present invention relates to an energy-saving single-runner hot-side bypass temperature control system and a method thereof, in particular to an energy-saving single runner heat-side bypass temperature control system and a method that can adjust the heat recovery amount or concentration when the concentration of volatile organic compounds (VOCs) becomes high, so that the During the treatment of organic waste gas, it can prevent the direct-fired incinerator (TO) from overheating due to too high furnace temperature, and even lead to shutdown. It is suitable for semiconductor industry, optoelectronic industry or chemical related industry. Organic waste gas treatment system or similar equipment.

按,目前在半導體產業或光電產業的製造生產過程中都會產生具有揮發性有機氣體(VOC),因此,在各廠區都會安裝處理揮發性有機氣體(VOC)的處理設備,以避免揮發性有機氣體(VOC)直接排入空氣中而造成空氣污染。而目前經由該處理設備所脫附的濃縮氣體大都是輸送到該焚燒爐來進行燃燒,再將燃燒後的氣體來輸送到煙囪來進行排放。 According to press, at present, volatile organic gases (VOC) are generated in the manufacturing process of semiconductor industry or optoelectronic industry. Therefore, treatment equipment for volatile organic gases (VOC) will be installed in each factory area to avoid volatile organic gases. (VOC) directly into the air and cause air pollution. At present, most of the concentrated gas desorbed by the treatment equipment is transported to the incinerator for combustion, and then the burned gas is transported to the chimney for discharge.

但是近年來,不管是中央政府或是各地方政府都對空氣汙染非常重視,也因此在煙囪的排放標準上訂定了有關大氣品質標準,同時將依國際管制趨勢發展,逐期檢討。 However, in recent years, both the central government and the local governments have attached great importance to air pollution, so they have formulated relevant air quality standards in the emission standards of chimneys, and will review them periodically in accordance with the development of international control trends.

因此,本發明人有鑑於上述缺失,期能提出一種具有提升有機廢氣處理效率的節能型單轉輪熱側旁通過溫控制系統及其方法,令使用者可輕易操作組裝,乃潛心研思、設計組製,以提供使用者便利性,為本發明人所欲研發之發明動機者。 Therefore, in view of the above deficiencies, the present inventor hopes to propose an energy-saving single-runner hot-side bypass temperature control system and method thereof, which can improve the efficiency of organic waste gas treatment, so that users can easily operate and assemble. The system is designed to provide user convenience and the motivation of the inventor to develop the invention.

本發明之主要目的,在於提供一種節能型單轉輪熱側旁通過溫控制系統及其方法,主要係用於有機廢氣處理系統,且設有一直燃式焚燒爐(TO),一第一熱交換器、一第二熱交換器、一第一冷側輸送管路、一吸附轉輪及一煙囪,並透過在該直燃式焚燒爐(TO)之爐膛係設有一熱側強排管路,且該熱側強排管路的另一端係與該第二熱交換器之第二熱側管路與該第一熱交換器之第一熱側管路之間相連處、或與該直燃式焚燒爐(TO)之出口之其中任一處連接,藉此,當揮發性有機化合物(VOCs)濃度變高時,能透過該熱側強排管路來調節該直燃式焚燒爐(TO)之爐膛的風量,以具有調節熱回收量或濃度之效能,使有機廢氣在處理時,能防止直燃式焚燒爐(TO)不會因爐溫太高而發生過溫之現象,甚至導致停機之情形發生,進而增加整體之實用性。 The main purpose of the present invention is to provide an energy-saving single runner hot side bypass temperature control system and method thereof, which are mainly used in organic waste gas treatment systems, and are provided with a direct-fired incinerator (TO), a first heat Exchanger, a second heat exchanger, a first cold side conveying pipeline, an adsorption runner and a chimney, and a hot side strong exhaust pipeline is provided through the furnace of the direct-fired incinerator (TO) , and the other end of the hot-side strong discharge pipe is connected with the second hot-side pipe of the second heat exchanger and the first hot-side pipe of the first heat exchanger, or with the direct The direct-fired incinerator (TO) is connected to any one of the outlets, so that when the concentration of volatile organic compounds (VOCs) becomes high, the direct-fired incinerator ( The air volume of the furnace of TO) has the effect of adjusting the amount of heat recovery or concentration, so that when the organic waste gas is treated, it can prevent the direct-fired incinerator (TO) from overheating due to too high furnace temperature, and even Situations that lead to downtime occur, thereby increasing overall utility.

本發明之另一目的,在於提供一種節能型單轉輪熱側旁通過溫控制系統及其方法,透過在該熱側強排管路係設有至少一調節風門,而該熱側強排管路的另一端係與該第二熱交換器之第二熱側管路與該第一熱交換器之第一熱側管路之間相連處、或與該直燃式焚燒爐(TO)之出口之其中任一處連接,以當揮發性有機化合物(VOCs)濃度變高時,能透過該熱側強排管路來調節該直燃式焚燒爐(TO)之爐膛的風量,並將部份焚燒之高溫氣體輸送到不同的熱交換器之熱側管路的相連接處,讓該熱側強排管路具有調節熱回收量或濃度之效能,使有機廢氣在處理時,能防止直燃式焚燒爐(TO)不會因爐溫太高而發生過溫之現象,甚至導致停機之情形發生,進而增加整體之使用性,進而增加整體之使用性。 Another object of the present invention is to provide an energy-saving single runner hot side bypass temperature control system and method thereof. The other end of the road is connected with the second hot side pipe of the second heat exchanger and the first hot side pipe of the first heat exchanger, or with the direct-fired incinerator (TO). Any one of the outlets is connected, so that when the concentration of volatile organic compounds (VOCs) becomes higher, the air volume of the furnace chamber of the direct-fired incinerator (TO) can be adjusted through the hot-side strong exhaust pipe, and the part of the outlet can be adjusted. The high temperature gas of the incineration is transported to the connection of the hot side pipes of different heat exchangers, so that the hot side strong exhaust pipe has the effect of adjusting the heat recovery amount or concentration, so that the organic waste gas can be prevented from being directly discharged during the treatment. The combustion type incinerator (TO) will not overheat due to too high furnace temperature, or even lead to shutdown, thereby increasing the overall usability, thereby increasing the overall usability.

為了能夠更進一步瞭解本發明之特徵、特點和技術內容,請參閱以下有關本發明之詳細說明與附圖,惟所附圖式僅提供參考與說明用,非用以限制本發明。 In order to further understand the features, characteristics and technical content of the present invention, please refer to the following detailed description of the present invention and the accompanying drawings, but the accompanying drawings are only for reference and description, and are not intended to limit the present invention.

10:直燃式焚燒爐(TO) 10: Direct-fired incinerator (TO)

101:爐頭 101: Stove

102:爐膛 102: Hearth

11:入口 11: Entrance

12:出口 12: Export

20:第一熱交換器 20: First heat exchanger

21:第一冷側管路 21: The first cold side pipeline

22:第一熱側管路 22: The first hot side pipeline

23:第一冷側輸送管路 23: The first cold side delivery pipeline

30:第二熱交換器 30: Second heat exchanger

31:第二冷側管路 31: Second cold side pipeline

32:第二熱側管路 32: Second hot side piping

60:吸附轉輪 60: Adsorption runner

601:吸附區 601: Adsorption zone

602:冷卻區 602: Cooling Zone

603:脫附區 603: Desorption zone

61:廢氣進氣管路 61: Exhaust gas intake line

611:廢氣連通管路 611: Exhaust gas communication line

6111:廢氣連通控制閥門 6111: Exhaust gas communication control valve

62:淨氣排放管路 62: Clean air discharge pipeline

621:淨氣連通管路 621: Clean air connection pipeline

6211:淨氣連通控制閥門 6211: Clean air connection control valve

63:冷卻氣進氣管路 63: Cooling air intake line

64:冷卻氣輸送管路 64: Cooling gas delivery pipeline

65:熱氣輸送管路 65: Hot gas delivery pipeline

66:脫附濃縮氣體管路 66: Desorption concentrated gas pipeline

661:風機 661: Fan

80:煙囪 80: Chimney

90:熱側強排管路 90: Hot side strong discharge pipeline

901:調節風門 901: Adjust the damper

S100:輸入待吸附之氣體 S100: Input the gas to be adsorbed

S200:輸入待吸附之氣體 S200: Input the gas to be adsorbed

S110:吸附轉輪進行吸附 S110: adsorption by the adsorption runner

S210:吸附轉輪進行吸附 S210: adsorption by the adsorption runner

S120:輸入冷卻氣體 S120: Input cooling gas

S220:輸入冷卻氣體 S220: Input cooling gas

S130:輸送熱氣脫附 S130: Transporting hot gas for desorption

S230:輸送熱氣脫附 S230: Transporting hot gas for desorption

S140:脫附濃縮氣體輸送 S140: Desorption enriched gas delivery

S240:脫附濃縮氣體輸送 S240: Delivery of Desorbed Concentrated Gas

S150:焚燒後之氣體輸送 S150: Gas delivery after incineration

S250:焚燒後之氣體輸送 S250: Gas delivery after incineration

S160:熱側強排管路調節 S160: Adjustment of hot side forced discharge pipeline

S260:熱側強排管路調節 S260: Hot Side Forced Discharge Pipeline Adjustment

S300:輸入待吸附之氣體 S300: Input the gas to be adsorbed

S400:輸入待吸附之氣體 S400: Input the gas to be adsorbed

S310:吸附轉輪進行吸附 S310: adsorption by the adsorption runner

S410:吸附轉輪進行吸附 S410: adsorption by the adsorption runner

S320:輸入冷卻氣體 S320: Input cooling gas

S420:輸入冷卻氣體 S420: Input cooling gas

S330:輸送熱氣脫附 S330: Transporting hot gas for desorption

S430:輸送熱氣脫附 S430: Transporting hot gas for desorption

S340:脫附濃縮氣體輸送 S340: Desorption Concentrated Gas Delivery

S440:脫附濃縮氣體輸送 S440: Desorption Concentrated Gas Delivery

S350:焚燒後之氣體輸送 S350: Gas delivery after incineration

S450:焚燒後之氣體輸送 S450: Gas delivery after incineration

S360:熱側強排管路調節 S360: Hot Side Forced Discharge Pipeline Adjustment

S460:熱側強排管路調節 S460: Hot Side Forced Discharge Pipeline Adjustment

第1圖係為本發明第一熱交換器設於該第二熱交換器右邊之第一種實施態樣具有熱側強排管路的系統架構示意圖。 Fig. 1 is a schematic diagram of the system structure of the first embodiment of the present invention, in which the first heat exchanger is arranged on the right side of the second heat exchanger and has a hot-side strong discharge pipeline.

第2圖係為本發明第一熱交換器設於該第二熱交換器右邊之第二種實施態樣具有熱側強排管路的系統架構示意圖。 Fig. 2 is a schematic diagram of the system structure of the second embodiment of the present invention, in which the first heat exchanger is arranged on the right side of the second heat exchanger and has a hot-side strong discharge pipeline.

第3圖係為本發明第一熱交換器設於該第二熱交換器左邊之第一種實施態樣具有熱側強排管路的系統架構示意圖。 Fig. 3 is a schematic diagram of the system structure of the first embodiment of the present invention, in which the first heat exchanger is disposed on the left side of the second heat exchanger and has a hot-side strong discharge pipeline.

第4圖係為本發明第一熱交換器設於該第二熱交換器左邊之第二種實施態樣具有熱側強排管路的系統架構示意圖。 FIG. 4 is a schematic diagram of the system structure of the second embodiment of the present invention, in which the first heat exchanger is disposed on the left side of the second heat exchanger and has a hot-side strong discharge pipeline.

第5圖係為本發明之第一種實施態樣的主要步驟流程圖。 FIG. 5 is a flow chart of the main steps of the first embodiment of the present invention.

第6圖係為本發明之第二種實施態樣的主要步驟流程圖。 FIG. 6 is a flow chart of the main steps of the second embodiment of the present invention.

第7圖係為本發明之第三種實施態樣的主要步驟流程圖。 FIG. 7 is a flow chart of the main steps of the third embodiment of the present invention.

第8圖係為本發明之第四種實施態樣的主要步驟流程圖。 FIG. 8 is a flow chart of the main steps of the fourth embodiment of the present invention.

請參閱第1~8圖,係為本發明實施例之示意圖,而本發明之節能型單轉輪熱側旁通過溫控制系統及其方法的最佳實施方式係運用於半導體產業、光電產業或化學相關產業的揮發有機廢氣處理系統或類似設備,主要是揮發性有機化合物(VOCs)濃度變高時,能具有調節熱回收量或 濃度之效能,使有機廢氣在處理時,能防止直燃式焚燒爐(TO)不會因爐溫太高而發生過溫之現象,甚至導致停機之情形發生。 Please refer to FIGS. 1 to 8, which are schematic diagrams of embodiments of the present invention, and the best embodiments of the energy-saving single-wheel hot-side bypass temperature control system and method thereof of the present invention are used in the semiconductor industry, the optoelectronic industry or the Volatile organic waste gas treatment systems or similar equipment in chemical-related industries, mainly when the concentration of volatile organic compounds (VOCs) increases, can adjust the amount of heat recovery or The effect of concentration can prevent the direct-fired incinerator (TO) from overheating due to too high furnace temperature during the treatment of organic waste gas, and even lead to shutdown.

而本發明之節能型單轉輪熱側旁通過溫控制系統,主要係包括有一直燃式焚燒爐(TO)10、一第一熱交換器20、一第二熱交換器30、一第一冷側輸送管路23、一吸附轉輪60及一煙囪80的組合設計(如第1圖至第4圖所示),其中該第一熱交換器20係設有第一冷側管路21及第一熱側管路22,該第二熱交換器30係設有第二冷側管路31及第二熱側管路32。另該直燃式焚燒爐(TO)10係設有一爐頭101及一爐膛102,該爐頭101係與該爐膛102係相通,且該第一熱交換器20及第二熱交換器30係分別設於該直燃式焚燒爐(TO)10內,而該直燃式焚燒爐(TO)10係設有入口11及出口12(如第1圖至第4圖所示),且該入口11係設於該爐頭101處,並該入口11係與該第一熱交換器20之第一冷側管路21的另一端連接,再者,該出口12則設於該爐膛102處,而該出口12係連接至該煙囪80,藉此,使該有機廢氣能由該入口11來進入該爐頭101內進行燃燒,再讓經過燃燒後之氣體能穿過該爐膛102並由該出口12來排出至煙囪80處進行排放,以具有節省能源之效能。 The energy-saving single-wheel hot-side bypass temperature control system of the present invention mainly includes a direct-fired incinerator (TO) 10, a first heat exchanger 20, a second heat exchanger 30, a first heat exchanger The combined design of the cold side conveying pipeline 23, an adsorption runner 60 and a chimney 80 (as shown in Figures 1 to 4), wherein the first heat exchanger 20 is provided with a first cold side pipeline 21 and the first hot side pipeline 22 , the second heat exchanger 30 is provided with a second cold side pipeline 31 and a second hot side pipeline 32 . In addition, the direct-fired incinerator (TO) 10 is provided with a burner head 101 and a furnace chamber 102, the burner head 101 is communicated with the furnace chamber 102, and the first heat exchanger 20 and the second heat exchanger 30 are connected with each other. They are respectively installed in the direct-fired incinerator (TO) 10, and the direct-fired incinerator (TO) 10 is provided with an inlet 11 and an outlet 12 (as shown in Figures 1 to 4), and the inlet 11 is set at the furnace head 101, and the inlet 11 is connected to the other end of the first cold side pipeline 21 of the first heat exchanger 20, and the outlet 12 is set at the furnace chamber 102, The outlet 12 is connected to the chimney 80 , thereby, the organic waste gas can enter the burner 101 through the inlet 11 for combustion, and the burned gas can pass through the hearth 102 and pass through the outlet 12 to be discharged to the chimney 80 for discharge, so as to have the effect of saving energy.

且該上述第一熱交換器20係具有兩種實施方式,其中第一種實施方式乃是將第一熱交換器20設於該第二熱交換器30右邊(如第1圖及第2圖所示),使該直燃式焚燒爐(TO)10之爐頭101係能將經過焚燒之高溫氣體先輸送到該第二熱交換器30之第二熱側管路32的一側以進行熱交換,之後再由該第二熱交換器30之第二熱側管路32的另一 側來將經過焚燒之高溫氣體再輸送到該第一熱交換器20之第一熱側管路22的一側以進行熱交換,最後由該第一熱交換器20之第一熱側管路22的另一側來輸送到該爐膛102之出口12(如第1圖及第2圖所示),再由該爐膛102之出口12來輸送到煙囪80,以透過該煙囪80來進行排放。 And the above-mentioned first heat exchanger 20 has two embodiments, wherein the first embodiment is to set the first heat exchanger 20 on the right side of the second heat exchanger 30 (as shown in FIG. 1 and FIG. 2 ). shown), so that the burner head 101 of the direct-fired incinerator (TO) 10 can firstly transport the incinerated high-temperature gas to one side of the second hot-side pipeline 32 of the second heat exchanger 30 for heat exchange, and then by the second heat exchanger 30 of the second hot side pipe The incinerated high temperature gas is transported to one side of the first hot side pipeline 22 of the first heat exchanger 20 for heat exchange, and finally the first hot side pipeline of the first heat exchanger 20 22 to be transported to the outlet 12 of the furnace 102 (as shown in Figures 1 and 2), and then transported to the chimney 80 from the outlet 12 of the furnace 102 to be discharged through the chimney 80.

再者,另第二種實施方式乃是將第一熱交換器20設於該第三熱交換器40左邊(如第3圖及第4圖所示),使該直燃式焚燒爐(TO)10之爐頭101係能將經過焚燒之高溫氣體先輸送到該第一熱交換器20之第一熱側管路22的一側以進行熱交換,且由該第一熱交換器20之第一熱側管路22的另一側來將經過焚燒之高溫氣體再輸送到該第二熱交換器30之第二熱側管路32的一側以進行熱交換,之後再由該第二熱交換器30之第二熱側管路32的另一側來將經過焚燒之高溫氣體再輸送到該爐膛102之出口12(如第3圖及第4圖所示),再由該爐膛102之出口12來輸送到煙囪80,以透過該煙囪80來進行排放。 Furthermore, another second embodiment is to set the first heat exchanger 20 on the left side of the third heat exchanger 40 (as shown in Fig. 3 and Fig. 4 ), so that the direct-fired incinerator (TO ) The burner 101 of 10 is capable of transporting the incinerated high-temperature gas to one side of the first hot-side pipeline 22 of the first heat exchanger 20 for heat exchange, and is passed through the first heat exchanger 20. The other side of the first hot side pipeline 22 is used to transport the incinerated high-temperature gas to one side of the second hot side pipeline 32 of the second heat exchanger 30 for heat exchange. The other side of the second hot-side pipeline 32 of the heat exchanger 30 is used to transport the incinerated high-temperature gas to the outlet 12 of the furnace 102 (as shown in Figures 3 and 4), and then the furnace 102 The outlet 12 is conveyed to the chimney 80 for discharge through the chimney 80 .

另本發明之吸附轉輪60係設有吸附區601、冷卻區602及脫附區603,該吸附轉輪60係連接有一廢氣進氣管路61、一淨氣排放管路62、一冷卻氣進氣管路63、一冷卻氣輸送管路64、一熱氣輸送管路65及一脫附濃縮氣體管路66,(如第1圖至第4圖所示)。其中該吸附轉輪60係為沸石濃縮轉輪或是其他材質之濃縮轉輪。 In addition, the adsorption runner 60 of the present invention is provided with an adsorption zone 601, a cooling zone 602 and a desorption zone 603, and the adsorption runner 60 is connected with an exhaust gas intake pipe 61, a clean air discharge pipe 62, and a cooling gas Intake pipeline 63, a cooling gas delivery pipeline 64, a hot gas delivery pipeline 65 and a desorption concentrated gas pipeline 66, (as shown in Figs. 1 to 4). The adsorption wheel 60 is a zeolite concentration wheel or a concentration wheel made of other materials.

其中該廢氣進氣管路61的一端係連接至該吸附轉輪60之吸附區601的一側,使該廢氣進氣管路61能將有機廢氣輸送到該吸附轉輪60之吸附區601的一側,而該淨氣排放管路62的一端係與該 吸附轉輪60之吸附區601的另一側連接,該淨氣排放管路62的另一端來與該煙囪80連接,且該淨氣排放管路62係設有一風機621(如第2圖及第4圖所示),使能透過該風機621來將該淨氣排管路62內的經過吸附後之氣體推拉到該煙囪80內以進行排放。 One end of the exhaust gas intake pipeline 61 is connected to one side of the adsorption zone 601 of the adsorption rotor 60 , so that the exhaust gas intake pipeline 61 can transport the organic exhaust gas to the adsorption zone 601 of the adsorption rotor 60 . one side, and one end of the clean air discharge pipe 62 is connected to the The other side of the adsorption zone 601 of the adsorption wheel 60 is connected, the other end of the clean gas discharge pipeline 62 is connected to the chimney 80, and the clean gas discharge pipeline 62 is provided with a fan 621 (as shown in Fig. 2 and As shown in FIG. 4 ), through the fan 621 , the adsorbed gas in the clean air exhaust line 62 can be pushed and pulled into the chimney 80 for discharge.

另該吸附轉輪60之冷卻區602的一側係連接該冷卻氣進氣管路63,以供氣體進入該吸附轉輪60之冷卻區602來進行冷卻使用(如第1圖至第4圖所示),而該吸附轉輪60之冷卻區602的另一側係連接該冷卻氣輸送管路64的一端,該冷卻氣輸送管路64的另一端則與該第二熱交換器30之第二冷側管路31的一端連接,以將進入該吸附轉輪60之冷卻區602後之氣體輸送到該第二熱交換器30內進行熱交換(如第1圖至第4圖所示),再者,該熱氣輸送管路65的一端係與該吸附轉輪60之脫附區603的另一側連接,且該熱氣輸送管路65的另一端係與該第二熱交換器30之第二冷側管路31的另一端連接,以能將經由該第二熱交換器30進行熱交換的高溫熱氣透過該熱氣輸送管路65來輸送到該吸附轉輪60之脫附區603來進行脫附使用。 In addition, one side of the cooling zone 602 of the adsorption wheel 60 is connected to the cooling gas inlet pipeline 63 for the gas to enter the cooling zone 602 of the adsorption wheel 60 for cooling (as shown in Figs. 1 to 4). shown), and the other side of the cooling zone 602 of the adsorption runner 60 is connected to one end of the cooling gas delivery pipeline 64, and the other end of the cooling gas delivery pipeline 64 is connected to the second heat exchanger 30. One end of the second cold side pipeline 31 is connected to transport the gas after entering the cooling zone 602 of the adsorption runner 60 into the second heat exchanger 30 for heat exchange (as shown in FIG. 1 to FIG. 4 ). ), and further, one end of the hot gas conveying line 65 is connected to the other side of the desorption zone 603 of the adsorption wheel 60, and the other end of the hot gas conveying line 65 is connected to the second heat exchanger 30 The other end of the second cold side pipeline 31 is connected, so that the high-temperature hot gas for heat exchange through the second heat exchanger 30 can be transported to the desorption zone 603 of the adsorption runner 60 through the hot gas transport pipeline 65 for desorption.

而上述該吸附轉輪60之冷卻區602係設有兩種實施方式,其中第一種實施方式為該吸附轉輪60之冷卻區602的一側所連接的冷卻氣進氣管路63乃是供新鮮空氣或外氣進入(如第1圖所示),透過該新鮮空氣或外氣來提供該吸附轉輪60之冷卻區602降溫用。另第二種實施方式係該廢氣進氣管路61係設有一廢氣連通管路611,而該廢氣連通管路611的另一端係與該冷卻氣進氣管路63連接(如第2圖及第4圖所示),以能透過該廢氣連通管路611來將該廢氣進氣管路6 1內的廢氣輸送到該吸附轉輪60之冷卻區602以進行降溫使用,另該廢氣連通管路611係設有一廢氣連通控制閥門6111,以控制該廢氣連通管路611的風量。 The above-mentioned cooling zone 602 of the adsorption wheel 60 is provided with two embodiments. The first embodiment is that the cooling gas intake pipe 63 connected to one side of the cooling zone 602 of the adsorption wheel 60 is For the entry of fresh air or outside air (as shown in FIG. 1 ), the cooling zone 602 of the adsorption wheel 60 is provided for cooling through the fresh air or outside air. Another second embodiment is that the exhaust gas intake pipe 61 is provided with an exhaust gas communication pipe 611, and the other end of the exhaust gas communication pipe 611 is connected to the cooling gas intake pipe 63 (as shown in FIG. 2 and 4), so that the exhaust gas intake line 6 can pass through the exhaust gas communication line 611 The waste gas in 1 is sent to the cooling zone 602 of the adsorption runner 60 for cooling use. In addition, the waste gas communication line 611 is provided with an waste gas communication control valve 6111 to control the air volume of the waste gas communication line 611 .

另該脫附濃縮氣體管路66的一端係與該吸附轉輪60之脫附區603的一側連接,而該脫附濃縮氣體管路66的另一端係與該第一熱交換器20之第一冷側管路21的一端連接,其中該第一熱交換器20之第一冷側管路21的另一端係與該第一冷側輸送管路23的一端連接,而該第一冷側輸送管路23的另一端則與該直燃式焚燒爐(TO)10之入口11連接,以能將經過高溫所脫附下來的脫附濃縮氣體能透過該脫附濃縮氣體管路66來輸送到該第一熱交換器20之第一冷側管路21的一端內,且由該第一熱交換器20之第一冷側管路21的另一端來輸送到該直燃式焚燒爐(TO)10之入口11內(如第1圖至第4圖所示),使能讓該直燃式焚燒爐(TO)10的爐頭101來進行高溫裂解,以能減少揮發性有機化合物。另該脫附濃縮氣體管路66係設有一風機661,以能將脫附濃縮氣體來推拉進入該第一熱交換器20之第一冷側管路21的一端內。 In addition, one end of the desorption concentrated gas pipeline 66 is connected to one side of the desorption zone 603 of the adsorption rotor 60 , and the other end of the desorption concentrated gas pipeline 66 is connected to the first heat exchanger 20 . One end of the first cold side pipeline 21 is connected, wherein the other end of the first cold side pipeline 21 of the first heat exchanger 20 is connected to one end of the first cold side conveying pipeline 23, and the first cold side pipeline 23 is connected to one end of the first cold side pipeline 23. The other end of the side conveying pipeline 23 is connected to the inlet 11 of the direct-fired incinerator (TO) 10, so that the desorbed concentrated gas desorbed by the high temperature can pass through the desorbed concentrated gas pipeline 66. It is transported to one end of the first cold side pipeline 21 of the first heat exchanger 20, and is transported to the direct-fired incinerator from the other end of the first cold side pipeline 21 of the first heat exchanger 20 In the inlet 11 of the (TO) 10 (as shown in Figures 1 to 4), the burner head 101 of the direct-fired incinerator (TO) 10 can be pyrolyzed to reduce volatile organic compounds . In addition, the desorption concentrated gas pipeline 66 is provided with a fan 661 to push and pull the desorption concentrated gas into one end of the first cold side pipeline 21 of the first heat exchanger 20 .

再者,本發明之節能型單轉輪熱側旁通過溫控制系統,主要是有二種的實施態樣,而該二種的實施態樣中的直燃式焚燒爐(TO)10、第一熱交換器20、第二熱交換器30、第一冷側輸送管路23、吸附轉輪60及煙囪80是採相同的設計,因此,上述的直燃式焚燒爐(TO)10、第一熱交換器20、第二熱交換器30、第一冷側輸送管路23、吸附轉輪60及煙囪80內容不在重複,請參考上述之說明內容。 Furthermore, the energy-saving single-wheel hot-side bypass temperature control system of the present invention mainly has two implementations, and in the two implementations, the direct-fired incinerator (TO) 10, the first The first heat exchanger 20, the second heat exchanger 30, the first cold side conveying pipeline 23, the adsorption runner 60 and the chimney 80 are of the same design. Therefore, the above-mentioned direct-fired incinerator (TO) 10, the first The content of the first heat exchanger 20 , the second heat exchanger 30 , the first cold side conveying pipeline 23 , the adsorption runner 60 and the chimney 80 will not be repeated, please refer to the above description.

其中第一種實施態樣(如第1圖及第3圖所示)之差異乃為 在該直燃式焚燒爐(TO)10之爐膛102係設有一熱側強排管路90,該熱側強排管路90的一端係與該直燃式焚燒爐(TO)10之爐膛102連接,而不管該第一熱交換器20設於該第二熱交換器30右邊(如第1圖所示)或是該第一熱交換器20設於該第二熱交換器30左邊(如第3圖所示)時,該熱側強排管路90的另一端皆與該第二熱交換器30之第二熱側管路32與該第一熱交換器20之第一熱側管路22之間相連處連接,其中該熱側強排管路90係設有至少一調節風門901,也可以配合該管路來設有兩個調節風門(圖未示),以透過該調節風門901來調控該熱側強排管路90的風量,因此,當揮發性有機化合物(VOCs)濃度變高時,能透過該熱側強排管路90來調節該直燃式焚燒爐(TO)10之爐膛102的風量,並將部份焚燒之高溫氣體輸送到該第二熱交換器30之第二熱側管路32與該第一熱交換器20之第一熱側管路22之間相連處,讓該熱側強排管路90具有調節熱回收量或濃度之效能,使有機廢氣在處理時,能防止直燃式焚燒爐(TO)10不會因爐溫太高而發生過溫之現象,甚至導致停機之情形發生。 The difference between the first implementation (as shown in Figures 1 and 3) is that The furnace chamber 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side strong exhaust pipe 90 , and one end of the hot-side strong exhaust pipe 90 is connected to the furnace chamber 102 of the direct-fired incinerator (TO) 10 connection, regardless of whether the first heat exchanger 20 is located to the right of the second heat exchanger 30 (as shown in FIG. 1 ) or the first heat exchanger 20 is located to the left of the second heat exchanger 30 (as shown in FIG. 1 ) 3), the other end of the hot-side strong discharge pipe 90 is connected to the second hot-side pipe 32 of the second heat exchanger 30 and the first hot-side pipe of the first heat exchanger 20 The pipes 22 are connected at the connection point, wherein the hot-side strong exhaust pipe 90 is provided with at least one damper 901, and two dampers (not shown) can also be provided in conjunction with the pipe to pass the damper 901. 901 to regulate the air volume of the hot side strong exhaust pipe 90, therefore, when the concentration of volatile organic compounds (VOCs) becomes high, the direct-fired incinerator (TO) can be adjusted through the hot side strong exhaust pipe 90 10 and the air volume of the furnace chamber 102, and part of the incinerated high-temperature gas is transported between the second hot side pipeline 32 of the second heat exchanger 30 and the first hot side pipeline 22 of the first heat exchanger 20 At the connection, the hot-side strong exhaust pipe 90 has the effect of adjusting the amount of heat recovery or concentration, so that when the organic waste gas is treated, it can prevent the direct-fired incinerator (TO) 10 from occurring due to too high furnace temperature. The phenomenon of temperature, and even lead to downtime.

另,第二種實施態樣(如第2圖及第4圖所示)之差異乃於該直燃式焚燒爐(TO)10之爐膛102係設有一熱側強排管路90,該熱側強排管路90的一端係與該直燃式焚燒爐(TO)10之爐膛102連接,而不管該第一熱交換器20設於該第二熱交換器30右邊(如第2圖所示)或是該第一熱交換器20設於該第二熱交換器30左邊(如第4圖所示)時,該熱側強排管路90的另一端皆與該直燃式焚燒爐(TO)10之出口12連接,其中該熱側強排管路90係設有至少一調節風門901,也可以配合 該管路來設有兩個調節風門(圖未示),以透過該調節風門901來調控該熱側強排管路90的風量,因此,當揮發性有機化合物(VOCs)濃度變高時,能透過該熱側強排管路90來調節該直燃式焚燒爐(TO)10之爐膛102的風量,並將部份焚燒之高溫氣體輸送到該直燃式焚燒爐(TO)10之出口12處,讓該熱側強排管路90具有調節熱回收量或濃度之效能,使有機廢氣在處理時,能防止直燃式焚燒爐(TO)10不會因爐溫太高而發生過溫之現象,甚至導致停機之情形發生。 In addition, the difference of the second embodiment (as shown in FIG. 2 and FIG. 4 ) is that the furnace chamber 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side strong exhaust pipe 90 . One end of the side strong exhaust pipe 90 is connected with the furnace chamber 102 of the direct-fired incinerator (TO) 10, regardless of whether the first heat exchanger 20 is located on the right side of the second heat exchanger 30 (as shown in FIG. 2 ). shown) or when the first heat exchanger 20 is located on the left side of the second heat exchanger 30 (as shown in FIG. 4 ), the other end of the hot-side strong exhaust pipe 90 is connected to the direct-fired incinerator (TO) 10 is connected to the outlet 12, wherein the hot-side strong exhaust pipe 90 is provided with at least one regulating damper 901, which can also be matched with The pipeline is provided with two dampers (not shown), so that the air volume of the hot-side strong exhaust pipeline 90 can be regulated through the damper 901. Therefore, when the concentration of volatile organic compounds (VOCs) becomes high, The air volume of the furnace chamber 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot-side strong exhaust pipe 90, and part of the incinerated high-temperature gas can be delivered to the outlet of the direct-fired incinerator (TO) 10 12, let the hot-side strong exhaust pipe 90 have the effect of adjusting the amount of heat recovery or concentration, so that when the organic waste gas is treated, it can prevent the direct-fired incinerator (TO) 10 from occurring due to too high furnace temperature. The phenomenon of temperature, and even lead to downtime.

而本發明之節能型單轉輪熱側旁通過溫控制方法,其主要係用於有機廢氣處理系統,且包括有一直燃式焚燒爐(TO)10、一第一熱交換器20、一第二熱交換器30、一第一冷側輸送管路23、一吸附轉輪60及一煙囪80的組合設計(如第1圖至第4圖所示),其中該第一熱交換器20係設有第一冷側管路21及第一熱側管路22,該第二熱交換器30係設有第二冷側管路31及第二熱側管路32,其中該第一冷側輸送管路23的一端係與該第一冷側管路21的另一端連接,該第一冷側輸送管路23的另一端係與該直燃式焚燒爐(TO)10之入口11連接。另該直燃式焚燒爐(TO)10係設有一爐頭101及一爐膛102,該爐頭101係與該爐膛102係相通,且該第一熱交換器20及第二熱交換器30係分別設於該直燃式焚燒爐(TO)10內,而該直燃式焚燒爐(TO)10係設有入口11及出口12(如第1圖至第4圖所示),且該入口11係設於該爐頭101處,並該入口11係與該第一熱交換器20之第一冷側管路21的另一端連接,再者,該出口12則設於該爐膛102處,而該出口12係連接至該煙囪80,藉此,使該有機廢氣能由該入口11來進入該爐頭10 1內進行燃燒,再讓經過燃燒後之氣體能穿過該爐膛102並由該出口12來排出至煙囪80處進行排放,以具有節省能源之效能。 The energy-saving single-wheel hot-side bypass temperature control method of the present invention is mainly used in an organic waste gas treatment system, and includes a direct-fired incinerator (TO) 10, a first heat exchanger 20, a first The combined design of two heat exchangers 30, a first cold side conveying pipeline 23, an adsorption runner 60 and a chimney 80 (as shown in Figs. 1 to 4), wherein the first heat exchanger 20 is a A first cold side pipeline 21 and a first hot side pipeline 22 are provided, and the second heat exchanger 30 is provided with a second cold side pipeline 31 and a second hot side pipeline 32, wherein the first cold side pipeline One end of the delivery pipeline 23 is connected to the other end of the first cold side pipeline 21 , and the other end of the first cold side delivery pipeline 23 is connected to the inlet 11 of the direct-fired incinerator (TO) 10 . In addition, the direct-fired incinerator (TO) 10 is provided with a burner head 101 and a furnace chamber 102, the burner head 101 is communicated with the furnace chamber 102, and the first heat exchanger 20 and the second heat exchanger 30 are connected with each other. They are respectively installed in the direct-fired incinerator (TO) 10, and the direct-fired incinerator (TO) 10 is provided with an inlet 11 and an outlet 12 (as shown in Figures 1 to 4), and the inlet 11 is set at the furnace head 101, and the inlet 11 is connected to the other end of the first cold side pipeline 21 of the first heat exchanger 20, and the outlet 12 is set at the furnace chamber 102, And the outlet 12 is connected to the chimney 80 so that the organic waste gas can enter the burner 10 through the inlet 11 Combustion is carried out in 1, and then the burned gas can pass through the furnace 102 and be discharged from the outlet 12 to the chimney 80 for discharge, so as to have the effect of saving energy.

另本發明之吸附轉輪60係設有吸附區601、冷卻區602及脫附區603,該吸附轉輪60係連接有一廢氣進氣管路61、一淨氣排放管路62、一冷卻氣進氣管路63、一冷卻氣輸送管路64、一熱氣輸送管路65及一脫附濃縮氣體管路66(如第1圖至第4圖所示)。其中該吸附轉輪60係為沸石濃縮轉輪或是其他材質之濃縮轉輪。 In addition, the adsorption runner 60 of the present invention is provided with an adsorption zone 601, a cooling zone 602 and a desorption zone 603, and the adsorption runner 60 is connected with an exhaust gas intake pipe 61, a clean air discharge pipe 62, and a cooling gas Intake pipeline 63, a cooling gas delivery pipeline 64, a hot gas delivery pipeline 65 and a desorption concentrated gas pipeline 66 (as shown in Figs. 1 to 4). The adsorption wheel 60 is a zeolite concentration wheel or a concentration wheel made of other materials.

而該控制方法的主要步驟(如第5圖所示)係包括:步驟S100輸入待吸附之氣體:將廢氣透過該廢氣進氣管路61的另一端來送入該吸附轉輪60之吸附區601的一側。而完成上述步驟S100後即進行下一步驟S110。 The main steps of the control method (as shown in FIG. 5 ) include: step S100 inputting the gas to be adsorbed: passing the exhaust gas through the other end of the exhaust gas inlet pipe 61 and sending it into the adsorption area of the adsorption wheel 60 side of 601. After the above step S100 is completed, the next step S110 is performed.

另,下一步進行的步驟S110吸附轉輪進行吸附:透過該吸附轉輪60之吸附區601進行吸附後,由該吸附轉輪60之吸附區601的另一側將吸附後之氣體透過該淨氣排放管路62的另一端來輸出。而完成上述步驟S110後即進行下一步驟S120。 In addition, in the next step S110, the adsorption wheel performs adsorption: after the adsorption is carried out through the adsorption zone 601 of the adsorption wheel 60, the gas after adsorption is passed through the other side of the adsorption zone 601 of the adsorption wheel 60 through the net The other end of the gas discharge line 62 is output. After the above step S110 is completed, the next step S120 is performed.

其中上述之步驟S110中的吸附轉輪60之吸附區601的另一側所連接該淨氣排放管路62,以透過該淨氣排放管路62的另一端來與該煙囪80連接,且該淨氣排放管路62係設有一風機621(如第2圖及第4圖所示),使能透過該風機621來將該淨氣排管路62內的經過吸附後之氣體推拉到該煙囪80內以進行排放。 Wherein the other side of the adsorption area 601 of the adsorption wheel 60 in the above-mentioned step S110 is connected to the clean gas discharge pipeline 62 so as to be connected to the chimney 80 through the other end of the clean gas discharge pipeline 62, and the A fan 621 (as shown in Figures 2 and 4) is installed in the clean air discharge line 62, so that the adsorbed gas in the clean air discharge line 62 can be pushed and pulled to the chimney through the fan 621 80 for discharge.

另,下一步進行的步驟S120輸入冷卻氣體:透過該冷卻氣進氣管路63的另一端來輸送冷卻氣至該吸附轉輪60之冷卻區602 進行冷卻,再透過該冷卻氣輸送管路64的另一端來將經過該吸附轉輪60之冷卻區602的冷卻氣輸送到該第二熱交換器30之第二冷側管路31的一端。而完成上述步驟S120後即進行下一步驟S130。 In addition, the next step S120 is to input cooling gas: the cooling gas is sent to the cooling area 602 of the adsorption wheel 60 through the other end of the cooling gas inlet pipe 63 . After cooling, the cooling gas passing through the cooling zone 602 of the adsorption runner 60 is delivered to one end of the second cold side pipeline 31 of the second heat exchanger 30 through the other end of the cooling gas delivery pipeline 64 . After the above step S120 is completed, the next step S130 is performed.

其中上述之步驟S120中的吸附轉輪60之冷卻區602係設有兩種實施方式,其中第一種實施方式為該吸附轉輪60之冷卻區602的一側所連接的冷卻氣進氣管路63乃是供新鮮空氣或外氣進入(如第1圖所示),透過該新鮮空氣或外氣來提供該吸附轉輪60之冷卻區602降溫用。另第二種實施方式係該廢氣進氣管路61係設有一廢氣連通管路611,而該廢氣連通管路611的另一端係與該冷卻氣進氣管路63連接(如第2圖及第4圖所示),以能透過該廢氣連通管路611來將該廢氣進氣管路61內的廢氣輸送到該吸附轉輪60之冷卻區602以進行降溫使用,另該廢氣連通管路611係設有一廢氣連通控制閥門6111,以控制該廢氣連通管路611的風量。 The cooling area 602 of the adsorption wheel 60 in the above-mentioned step S120 has two implementations, wherein the first implementation is the cooling air intake pipe connected to one side of the cooling area 602 of the adsorption wheel 60 The passage 63 is for the entry of fresh air or outside air (as shown in FIG. 1 ), and the cooling zone 602 of the adsorption wheel 60 is provided for cooling through the fresh air or outside air. Another second embodiment is that the exhaust gas intake pipe 61 is provided with an exhaust gas communication pipe 611, and the other end of the exhaust gas communication pipe 611 is connected to the cooling gas intake pipe 63 (as shown in FIG. 2 and 4), so that the exhaust gas in the exhaust gas inlet pipe 61 can be transported to the cooling zone 602 of the adsorption runner 60 through the exhaust gas communication pipe 611 for cooling use, and the exhaust gas communication pipe 611 is provided with an exhaust gas communication control valve 6111 to control the air volume of the exhaust gas communication line 611 .

另,下一步進行的步驟S130輸送熱氣脫附:透過與第二熱交換器30之第二冷側管路31的另一端所連接的熱氣輸送管路65來將熱氣輸送到該吸附轉輪60之脫附區603進行脫附,再透過該脫附濃縮氣體管路66的另一端來將脫附濃縮氣體輸送到第一熱交換器20之第一冷側管路21的一端。而完成上述步驟S130後即進行下一步驟S140。 In addition, the next step S130 is to transport hot gas for desorption: the hot gas is transported to the adsorption runner 60 through the hot gas transport pipe 65 connected to the other end of the second cold side pipe 31 of the second heat exchanger 30 The desorption zone 603 is desorbed, and then the desorbed concentrated gas is sent to one end of the first cold side pipeline 21 of the first heat exchanger 20 through the other end of the desorbed concentrated gas pipeline 66 . After the above step S130 is completed, the next step S140 is performed.

其中上述之步驟S130中的脫附濃縮氣體管路66係設有一風機661(如第2圖及第4圖所示),以能將脫附濃縮氣體來推拉進入該第一熱交換器20之第一冷側管路21內。 The desorption concentrated gas pipeline 66 in the above-mentioned step S130 is provided with a fan 661 (as shown in FIG. 2 and FIG. 4 ), so that the desorption concentrated gas can be pushed and pulled into the first heat exchanger 20 . Inside the first cold side pipeline 21 .

另,下一步進行的步驟S140脫附濃縮氣體輸送:該脫附濃縮氣體再透過該第一熱交換器20之第一冷側管路21的另一端所連接的第一冷側輸送管路23來輸送到該直燃式焚燒爐(TO)10之入口11。而完成上述步驟S140後即進行下一步驟S150。 In addition, in the next step S140, the desorbed and concentrated gas is transported: the desorbed and concentrated gas passes through the first cold-side transport pipeline 23 connected to the other end of the first cold-side pipeline 21 of the first heat exchanger 20. to be transported to the inlet 11 of the direct-fired incinerator (TO) 10 . After the above step S140 is completed, the next step S150 is performed.

另,下一步進行的步驟S150焚燒後之氣體輸送:將該直燃式焚燒爐(TO)10之爐頭101所燃燒後而產生的焚燒後之氣體輸送到該第二熱交換器30之第二熱側管路32的一端,再由該第二熱交換器30之第二熱側管路32的另一端輸送到該第一熱交換器20之第一熱側管路22的一端,最後由該第一熱交換器20之第一熱側管路22的另一端輸送到該直燃式焚燒爐(TO)10之出口12。而完成上述步驟S150後即進行下一步驟S160。 In addition, in the next step S150, the gas delivery after incineration: the gas after incineration produced by the combustion of the burner head 101 of the direct-fired incinerator (TO) 10 is delivered to the second heat exchanger 30. One end of the second hot-side pipe 32 is then transported from the other end of the second hot-side pipe 32 of the second heat exchanger 30 to one end of the first hot-side pipe 22 of the first heat exchanger 20, and finally The other end of the first hot-side pipeline 22 of the first heat exchanger 20 is sent to the outlet 12 of the direct-fired incinerator (TO) 10 . After the above step S150 is completed, the next step S160 is performed.

其中上述之步驟S150中的直燃式焚燒爐(TO)10之爐頭101係能將經過焚燒之高溫氣體先輸送到該第二熱交換器30之第二熱側管路32的一側以進行熱交換(如第1圖所示),之後再由該第二熱交換器30之第二熱側管路32的另一側來將經過焚燒之高溫氣體再輸送到該第一熱交換器20之第一熱側管路22的一側以進行熱交換,最後由該第一熱交換器20之第一熱側管路22的另一側來輸送到該爐膛102之出口12,再由該爐膛102之出口12來輸送到煙囪80,以透過該煙囪80來進行排放。 The burner head 101 of the direct-fired incinerator (TO) 10 in the above-mentioned step S150 can transport the incinerated high-temperature gas to one side of the second hot-side pipeline 32 of the second heat exchanger 30 to Perform heat exchange (as shown in Figure 1), and then the incinerated high-temperature gas is sent to the first heat exchanger from the other side of the second hot side pipeline 32 of the second heat exchanger 30 One side of the first hot side pipeline 22 of the first heat exchanger 20 is used for heat exchange, and finally the other side of the first hot side pipeline 22 of the first heat exchanger 20 is transported to the outlet 12 of the furnace 102, and then sent to the outlet 12 of the furnace 102 by the other side. The outlet 12 of the furnace 102 is conveyed to the chimney 80 for discharge through the chimney 80 .

另,下一步進行的步驟S160熱側強排管路調節:該直燃式焚燒爐(TO)10之爐膛102係設有一熱側強排管路90,該熱側強排管路90的一端係與該直燃式焚燒爐(TO)10之爐膛102連接,該熱側強排 管路90的另一端係與該第二熱交換器30之第二熱側管路32與該第一熱交換器20之第一熱側管路22之間相連處連接,該熱側強排管路90係設有至少一調節風門901,以透過該熱側強排管路90來進行調節該直燃式焚燒爐(TO)10之爐膛102的風量。 In addition, the next step S160 is to adjust the hot-side forced discharge pipeline: the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced-discharge pipeline 90, and one end of the hot-side forced-discharge pipeline 90 is provided. It is connected with the furnace chamber 102 of the direct-fired incinerator (TO) 10, and the hot side is strongly discharged. The other end of the pipeline 90 is connected to the connection between the second hot side pipeline 32 of the second heat exchanger 30 and the first hot side pipeline 22 of the first heat exchanger 20, and the hot side is strongly discharged The pipeline 90 is provided with at least one regulating damper 901 to adjust the air volume of the furnace chamber 102 of the direct-fired incinerator (TO) 10 through the hot-side strong exhaust pipeline 90 .

其中上述之步驟S160中該熱側強排管路90的一端係與該直燃式焚燒爐(TO)10之爐膛102連接,而該熱側強排管路90的另一端係與該第二熱交換器30之第二熱側管路32與該第一熱交換器20之第一熱側管路22之間相連處連接,其中該熱側強排管路90係設有至少一調節風門901,也可以配合該管路來設有兩個調節風門(圖未示),以透過該調節風門901來調控該熱側強排管路90的風量,因此,當揮發性有機化合物(VOCs)濃度變高時,能透過該熱側強排管路90來調節該直燃式焚燒爐(TO)10之爐膛102的風量,並將部份焚燒之高溫氣體輸送到該第二熱交換器30之第二熱側管路32與該第一熱交換器20之第一熱側管路22之間相連處,讓該熱側強排管路90具有調節熱回收量或濃度之效能,使有機廢氣在處理時,能防止直燃式焚燒爐(TO)10不會因爐溫太高而發生過溫之現象,甚至導致停機之情形發生。 In the above step S160, one end of the hot-side strong exhaust pipe 90 is connected to the furnace chamber 102 of the direct-fired incinerator (TO) 10, and the other end of the hot-side strong exhaust pipe 90 is connected to the second The second hot-side pipe 32 of the heat exchanger 30 is connected to the first hot-side pipe 22 of the first heat exchanger 20, wherein the hot-side strong discharge pipe 90 is provided with at least one damper 901, two dampers (not shown in the figure) can also be arranged in conjunction with the pipeline, so as to adjust the air volume of the hot-side strong exhaust pipeline 90 through the damper 901. Therefore, when volatile organic compounds (VOCs) When the concentration becomes high, the air volume of the furnace chamber 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot-side strong exhaust pipe 90, and part of the incinerated high-temperature gas can be sent to the second heat exchanger 30 The connection between the second hot-side pipeline 32 and the first hot-side pipeline 22 of the first heat exchanger 20 allows the hot-side strong discharge pipeline 90 to have the effect of adjusting the amount or concentration of heat recovery, so that the organic When the waste gas is treated, it can prevent the direct-fired incinerator (TO) 10 from overheating due to too high furnace temperature, and even lead to shutdown.

再者,本發明之節能型單轉輪熱側旁通過溫控制方法,主要是有四種的實施態樣,而第一種實施態樣(如第5圖所示)的步驟S100輸入待吸附之氣體、步驟S110吸附轉輪進行吸附、S120輸入冷卻氣體、步驟S130輸送熱氣脫附、步驟S140脫附濃縮氣體輸送、步驟S150焚燒後之氣體輸送及步驟S160熱側強排管路調節,已於上述提出說明,請參考上述之說明內容。 Furthermore, the energy-saving single-wheel hot-side bypass temperature control method of the present invention mainly has four implementations, and the first implementation (as shown in FIG. 5 ) in step S100 inputs the input to be adsorbed The gas, step S110 adsorption runner for adsorption, S120 input cooling gas, step S130 delivery hot gas desorption, step S140 desorption concentrated gas delivery, step S150 gas delivery after incineration and step S160 hot side forced discharge pipeline adjustment, have been For the above description, please refer to the above description.

另第二種實施態樣(如第6圖所示)中的步驟S200輸入待吸附之氣體、步驟S210吸附轉輪進行吸附、S220輸入冷卻氣體、步驟S230輸送熱氣脫附、步驟S240脫附濃縮氣體輸送及步驟S250焚燒後之氣體輸送,與第三種實施態樣(如第7圖所示)中的步驟S300輸入待吸附之氣體、步驟S310吸附轉輪進行吸附、S320輸入冷卻氣體、步驟S330輸送熱氣脫附、步驟S340脫附濃縮氣體輸送及步驟S350焚燒後之氣體輸送,另第四實施態樣(如第8圖所示)中的步驟S400輸入待吸附之氣體、步驟S410吸附轉輪進行吸附、S420輸入冷卻氣體、步驟S430輸送熱氣脫附、步驟S440脫附濃縮氣體輸送及步驟S450焚燒後之氣體輸送,都是採用與第一種實施態樣(如第5圖所示)中的步驟S100輸入待吸附之氣體、步驟S110吸附轉輪進行吸附、S120輸入冷卻氣體、步驟S130輸送熱氣脫附、步驟S140脫附濃縮氣體輸送、步驟S150焚燒後之氣體輸送之相同的設計,僅差異在於步驟S150焚燒後之氣體輸送及步驟S160熱側強排管路調節之內容。 In the second embodiment (as shown in FIG. 6 ), the gas to be adsorbed is input in step S200 , the adsorption wheel is adsorbed in step S210 , the cooling gas is input in step S220 , the hot gas is conveyed for desorption in step S230 , and the desorption concentration in step S240 The gas delivery and the gas delivery after the incineration in step S250 are the same as the step S300 of the third embodiment (as shown in FIG. 7) to input the gas to be adsorbed, the step S310 to adsorb the runner for adsorption, the step S320 to input the cooling gas, and the step S330 delivers hot gas desorption, step S340 delivers desorbed concentrated gas, and step S350 delivers gas after incineration. In addition, in step S400 of the fourth embodiment (as shown in FIG. 8 ), the gas to be adsorbed is inputted in step S400, and the adsorbed gas is transferred in step S410. Carrying out adsorption, inputting cooling gas in S420, conveying hot gas desorption in step S430, conveying desorbed concentrated gas in step S440, and conveying gas after incineration in step S450, all of which are the same as those in the first embodiment (as shown in Fig. 5). The same design of step S100 inputting the gas to be adsorbed, step S110 adsorbing the runner for adsorption, S120 inputting cooling gas, step S130 conveying hot gas desorption, step S140 desorbing concentrated gas conveying, step S150 gas conveying after incineration, The only difference lies in the gas delivery after the incineration in step S150 and the content of the adjustment of the hot-side forced exhaust pipeline in step S160.

因此,上述與步驟S100輸入待吸附之氣體、步驟S110吸附轉輪進行吸附、S120輸入冷卻氣體、步驟S130輸送熱氣脫附、步驟S140脫附濃縮氣體輸送之相同的內容不在重複,請參考上述之說明內容。下列將針對第二種實施態樣(如第6圖所示)中的步驟S250焚燒後之氣體輸送及步驟S260熱側強排管路調節、第三種實施態樣(如第7圖所示)中的步驟S350焚燒後之氣體輸送及步驟S360熱側強排管路調節及第四種實施態樣(如第8圖所示)中的步驟S450 焚燒後之氣體輸送及步驟S460熱側強排管路調節來進行說明。 Therefore, the same content as the step S100 to input the gas to be adsorbed, the step S110 to adsorb the runner for adsorption, the S120 to input the cooling gas, the step S130 to convey the hot gas for desorption, and the step S140 to convey the desorbed concentrated gas will not be repeated. Please refer to the above. Description content. The following will focus on the second embodiment (as shown in Figure 6), the gas delivery after incineration in step S250 and the adjustment of the hot-side forced discharge pipeline in step S260, and the third embodiment (as shown in Figure 7) ) in step S350 of gas delivery after incineration and step S360 of hot-side forced discharge pipeline adjustment and step S450 in the fourth embodiment (as shown in FIG. 8 ) The gas transportation after incineration and the adjustment of the hot-side forced exhaust pipeline in step S460 will be described.

而第二種實施態樣(如第6圖所示)之差異乃為步驟S250焚燒後之氣體輸送:將該直燃式焚燒爐(TO)10之爐頭101所燃燒後而產生的焚燒後之氣體輸送到該第二熱交換器30之第二熱側管路32的一端,再由該第二熱交換器30之第二熱側管路32的另一端輸送到該第一熱交換器20之第一熱側管路22的一端,最後由該第一熱交換器20之第一熱側管路22的另一端輸送到該直燃式焚燒爐(TO)10之出口12。 The difference of the second embodiment (as shown in FIG. 6 ) is the gas delivery after the incineration in step S250 : the incineration gas generated after the burner 101 of the direct-fired incinerator (TO) 10 is burned. The gas is sent to one end of the second hot side pipeline 32 of the second heat exchanger 30, and then sent to the first heat exchanger from the other end of the second hot side pipeline 32 of the second heat exchanger 30 One end of the first hot side pipeline 22 of the first heat exchanger 20 is finally transported to the outlet 12 of the direct-fired incinerator (TO) 10 from the other end of the first hot side pipeline 22 of the first heat exchanger 20 .

其中上述之步驟S250中直燃式焚燒爐(TO)10之爐頭101係能將經過焚燒之高溫氣體先輸送到該第二熱交換器30之第二熱側管路32的一側以進行熱交換(如第2圖所示),之後再由該第二熱交換器30之第二熱側管路32的另一側來將經過焚燒之高溫氣體再輸送到該第一熱交換器20之第一熱側管路22的一側以進行熱交換,最後由該第一熱交換器20之第一熱側管路22的另一側來輸送到該爐膛102之出口12,再由該爐膛102之出口12來輸送到煙囪80,以透過該煙囪80來進行排放。 The burner head 101 of the direct-fired incinerator (TO) 10 in the above-mentioned step S250 can firstly transport the incinerated high-temperature gas to one side of the second hot-side pipeline 32 of the second heat exchanger 30 for Heat exchange (as shown in FIG. 2 ), and then the incinerated high temperature gas is sent to the first heat exchanger 20 from the other side of the second hot side pipeline 32 of the second heat exchanger 30 One side of the first hot-side pipeline 22 of the first heat exchanger 20 is used for heat exchange, and finally the other side of the first hot-side pipeline 22 of the first heat exchanger 20 is transported to the outlet 12 of the furnace 102, and then sent to the outlet 12 of the furnace 102 by the The outlet 12 of the furnace 102 is conveyed to the chimney 80 for discharge therethrough.

而步驟S260熱側強排管路調節:該直燃式焚燒爐(TO)10之爐膛102係設有一熱側強排管路90,該熱側強排管路90的一端係與該直燃式焚燒爐(TO)10之爐膛102連接,該熱側強排管路90的另一端係與該直燃式焚燒爐(TO)10之出口12連接,該熱側強排管路90係設有至少一調節風門901,以透過該熱側強排管路90來進行調節該直燃式焚燒爐(TO)10之爐膛102的風量。 In step S260, the hot-side forced discharge pipeline is adjusted: the furnace chamber 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced-discharge pipeline 90, and one end of the hot-side forced-discharge pipeline 90 is connected to the direct-fired incinerator (TO) 10. The furnace chamber 102 of the type incinerator (TO) 10 is connected, and the other end of the hot side strong discharge pipeline 90 is connected with the outlet 12 of the direct-fired incinerator (TO) 10, and the hot side strong discharge pipeline 90 is provided with There is at least one regulating damper 901 for regulating the air volume of the furnace chamber 102 of the direct-fired incinerator (TO) 10 through the hot-side strong exhaust pipe 90 .

其中上述之步驟S260中該熱側強排管路90的一端係 與該直燃式焚燒爐(TO)10之爐膛102連接,而該熱側強排管路90的另一端係與該直燃式焚燒爐(TO)10之出口12連接,其中該熱側強排管路90係設有至少一調節風門901,也可以配合該管路來設有兩個調節風門(圖未示),以透過該調節風門901來調控該熱側強排管路90的風量,因此,當揮發性有機化合物(VOCs)濃度變高時,能透過該熱側強排管路90來調節該直燃式焚燒爐(TO)10之爐膛102的風量,並將部份焚燒之高溫氣體輸送到該直燃式焚燒爐(TO)10之出口12處,讓該熱側強排管路90具有調節熱回收量或濃度之效能,使有機廢氣在處理時,能防止直燃式焚燒爐(TO)10不會因爐溫太高而發生過溫之現象,甚至導致停機之情形發生。 In the above step S260, one end of the hot-side strong discharge pipeline 90 is It is connected with the furnace chamber 102 of the direct-fired incinerator (TO) 10, and the other end of the hot-side strong discharge pipeline 90 is connected with the outlet 12 of the direct-fired incinerator (TO) 10, wherein the hot side is strong The exhaust pipe 90 is provided with at least one damper 901, and two dampers (not shown) can also be provided in conjunction with the pipe, so as to adjust the air volume of the hot-side strong exhaust pipe 90 through the damper 901 Therefore, when the concentration of volatile organic compounds (VOCs) becomes high, the air volume of the furnace chamber 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot-side strong exhaust pipe 90, and part of the incinerator can be The high-temperature gas is sent to the outlet 12 of the direct-fired incinerator (TO) 10, so that the hot-side strong exhaust pipe 90 has the effect of adjusting the amount of heat recovery or concentration, so that the organic waste gas can be treated to prevent direct-fired The incinerator (TO) 10 will not be overheated due to too high furnace temperature, or even lead to shutdown.

另第三種實施態樣(如第7圖所示)之差異乃為步驟S350焚燒後之氣體輸送:將該直燃式焚燒爐(TO)10之爐頭101所燃燒後而產生的焚燒後之氣體輸送到該第一熱交換器20之第一熱側管路22的一端,且由該第一熱交換器20之第一熱側管路22的另一端輸送到該第二熱交換器30之第二熱側管路32的一端,再由該第二熱交換器30之第二熱側管路32的另一端輸送到該直燃式焚燒爐(TO)10之出口12。 The difference of the third embodiment (as shown in FIG. 7 ) is the gas delivery after the incineration in step S350: the incineration gas generated after the burner 101 of the direct-fired incinerator (TO) 10 is burned. The gas is delivered to one end of the first hot side pipe 22 of the first heat exchanger 20, and is delivered to the second heat exchanger from the other end of the first hot side pipe 22 of the first heat exchanger 20 One end of the second hot side pipeline 32 of the second heat exchanger 30 is then transported to the outlet 12 of the direct-fired incinerator (TO) 10 from the other end of the second hot side pipeline 32 of the second heat exchanger 30 .

其中上述之步驟S350中直燃式焚燒爐(TO)10之爐頭101係能將經過焚燒之高溫氣體先輸送到該第一熱交換器20之第一熱側管路22的一側以進行熱交換(如第3圖所示),且由該第一熱交換器20之第一熱側管路22的另一側來將經過焚燒之高溫氣體再輸送到該第二熱交換器30之第二熱側管路32的一側以進行熱交換,之後再由該第二熱交換器30之第二熱側管路32的另一側來將經過焚燒之高溫氣體再輸 送到該爐膛102之出口12,再由該爐膛102之出口12來輸送到煙囪80,以透過該煙囪80來進行排放。 The burner head 101 of the direct-fired incinerator (TO) 10 in the above-mentioned step S350 can firstly transport the incinerated high-temperature gas to one side of the first hot-side pipeline 22 of the first heat exchanger 20 for processing. Heat exchange (as shown in FIG. 3 ), and the incinerated high temperature gas is transported to the second heat exchanger 30 from the other side of the first hot side pipeline 22 of the first heat exchanger 20 One side of the second hot-side pipeline 32 is used for heat exchange, and then the incinerated high-temperature gas is re-transported from the other side of the second hot-side pipeline 32 of the second heat exchanger 30 It is sent to the outlet 12 of the furnace 102, and then conveyed to the chimney 80 from the outlet 12 of the furnace 102, so as to be discharged through the chimney 80.

而步驟S360熱側強排管路調節:該直燃式焚燒爐(TO)10之爐膛102係設有一熱側強排管路90,該熱側強排管路90的一端係與該直燃式焚燒爐(TO)10之爐膛102連接,該熱側強排管路90的另一端係與該第一熱交換器20之第一熱側管路22與該第二熱交換器30之第二熱側管路32之間相連處連接,該熱側強排管路90係設有至少一調節風門901,以透過該熱側強排管路90來進行調節該直燃式焚燒爐(TO)10之爐膛102的風量。 In step S360, the hot-side forced discharge pipeline is adjusted: the furnace chamber 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced-discharge pipeline 90, and one end of the hot-side forced-discharge pipeline 90 is connected to the direct-fired incinerator (TO) 10. The furnace chamber 102 of the type incinerator (TO) 10 is connected, and the other end of the hot side strong discharge pipe 90 is connected with the first hot side pipe 22 of the first heat exchanger 20 and the first hot side pipe 22 of the second heat exchanger 30 The two hot-side pipes 32 are connected at the connection point, and the hot-side forced exhaust pipe 90 is provided with at least one regulating damper 901 to adjust the direct-fired incinerator (TO) through the hot-side forced exhaust pipe 90 ) 10 of the air volume of the furnace 102.

其中上述之步驟S360中該熱側強排管路90的一端係與該直燃式焚燒爐(TO)10之爐膛102連接,而該熱側強排管路90的另一端係與該第一熱交換器20之第一熱側管路22與該第二熱交換器30之第二熱側管路32之間相連處連接,其中該熱側強排管路90係設有至少一調節風門901,也可以配合該管路來設有兩個調節風門(圖未示),以透過該調節風門901來調控該熱側強排管路90的風量,因此,當揮發性有機化合物(VOCs)濃度變高時,能透過該熱側強排管路90來調節該直燃式焚燒爐(TO)10之爐膛102的風量,並將部份焚燒之高溫氣體輸送到該第一熱交換器20之第一熱側管路22與該第二熱交換器30之第二熱側管路32之間相連處,讓該熱側強排管路90具有調節熱回收量或濃度之效能,使有機廢氣在處理時,能防止直燃式焚燒爐(TO)10不會因爐溫太高而發生過溫之現象,甚至導致停機之情形發生。 In the above-mentioned step S360, one end of the hot-side strong exhaust pipe 90 is connected to the furnace chamber 102 of the direct-fired incinerator (TO) 10, and the other end of the hot-side strong exhaust pipe 90 is connected to the first The first hot-side pipeline 22 of the heat exchanger 20 is connected with the second hot-side pipeline 32 of the second heat exchanger 30, wherein the hot-side strong exhaust pipeline 90 is provided with at least one damper 901, two dampers (not shown in the figure) can also be arranged in conjunction with the pipeline, so as to adjust the air volume of the hot-side strong exhaust pipeline 90 through the damper 901. Therefore, when volatile organic compounds (VOCs) When the concentration becomes higher, the air volume of the furnace chamber 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot-side strong exhaust pipe 90, and part of the incinerated high-temperature gas can be sent to the first heat exchanger 20 The connection between the first hot-side pipe 22 and the second hot-side pipe 32 of the second heat exchanger 30 allows the hot-side strong discharge pipe 90 to have the effect of adjusting the amount of heat recovery or concentration, so that the organic When the waste gas is treated, it can prevent the direct-fired incinerator (TO) 10 from overheating due to too high furnace temperature, and even lead to shutdown.

再者,第四種實施態樣(如第8圖所示)之差異乃為步驟S 450焚燒後之氣體輸送:將該直燃式焚燒爐(TO)10之爐頭101所燃燒後而產生的焚燒後之氣體輸送到該第一熱交換器20之第一熱側管路22的一端,且由該第一熱交換器20之第一熱側管路22的另一端輸送到該第二熱交換器30之第二熱側管路32的一端,再由該第二熱交換器30之第二熱側管路32的另一端輸送到該直燃式焚燒爐(TO)10之出口12。 Furthermore, the difference of the fourth implementation form (as shown in FIG. 8 ) is step S 450 Gas delivery after incineration: The gas after incineration produced by the combustion of the burner 101 of the direct-fired incinerator (TO) 10 is delivered to the first hot side pipeline 22 of the first heat exchanger 20. one end of the first hot-side pipe 22 of the first heat exchanger 20 is transported to one end of the second hot-side pipe 32 of the second heat exchanger 30, and then passed through the second heat exchanger 30. The other end of the second hot side pipeline 32 of 30 is delivered to the outlet 12 of the direct-fired incinerator (TO) 10 .

其中上述之步驟S450中直燃式焚燒爐(TO)10之爐頭101係能將經過焚燒之高溫氣體先輸送到該第一熱交換器20之第一熱側管路22的一側以進行熱交換(如第4圖所示),且由該第一熱交換器20之第一熱側管路22的另一側來將經過焚燒之高溫氣體再輸送到該第二熱交換器30之第二熱側管路32的一側以進行熱交換,之後再由該第二熱交換器30之第二熱側管路32的另一側來將經過焚燒之高溫氣體再輸送到該爐膛102之出口12,再由該爐膛102之出口12來輸送到煙囪80,以透過該煙囪80來進行排放。 The burner head 101 of the direct-fired incinerator (TO) 10 in the above-mentioned step S450 is capable of delivering the incinerated high-temperature gas to one side of the first hot-side pipeline 22 of the first heat exchanger 20 for processing. Heat exchange (as shown in FIG. 4 ), and the incinerated high temperature gas is transported to the second heat exchanger 30 from the other side of the first hot side pipeline 22 of the first heat exchanger 20 One side of the second hot side pipeline 32 is used for heat exchange, and then the incinerated high temperature gas is transported to the furnace 102 from the other side of the second hot side pipeline 32 of the second heat exchanger 30 The outlet 12 of the furnace 102 is then transported to the chimney 80 through the chimney 80 for discharge.

而步驟S460熱側強排管路調節:該直燃式焚燒爐(TO)10之爐膛102係設有一熱側強排管路90,該熱側強排管路90的一端係與該直燃式焚燒爐(TO)10之爐膛102連接,該熱側強排管路90的另一端係與該直燃式焚燒爐(TO)10之出口12連接,該熱側強排管路90係設有至少一調節風門901,以透過該熱側強排管路90來進行調節該直燃式焚燒爐(TO)10之爐膛102的風量。 In step S460, the hot-side forced discharge pipeline is adjusted: the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced-discharge pipeline 90, and one end of the hot-side forced-discharge pipeline 90 is connected to the direct-fired incinerator (TO) 10. The furnace chamber 102 of the type incinerator (TO) 10 is connected, and the other end of the hot side strong discharge pipeline 90 is connected with the outlet 12 of the direct-fired incinerator (TO) 10, and the hot side strong discharge pipeline 90 is provided with There is at least one regulating damper 901 for regulating the air volume of the furnace chamber 102 of the direct-fired incinerator (TO) 10 through the hot-side strong exhaust pipe 90 .

其中上述之步驟S460中該熱側強排管路90的一端係與該直燃式焚燒爐(TO)10之爐膛102連接,而該熱側強排管路90的另一端係與該直燃式焚燒爐(TO)10之出口12連接,其中該熱側強排管路9 0係設有至少一調節風門901,也可以配合該管路來設有兩個調節風門(圖未示),以透過該調節風門901來調控該熱側強排管路90的風量,因此,當揮發性有機化合物(VOCs)濃度變高時,能透過該熱側強排管路90來調節該直燃式焚燒爐(TO)10之爐膛102的風量,並將部份焚燒之高溫氣體輸送到該直燃式焚燒爐(TO)10之出口12處,讓該熱側強排管路90具有調節熱回收量或濃度之效能,使有機廢氣在處理時,能防止直燃式焚燒爐(TO)10不會因爐溫太高而發生過溫之現象,甚至導致停機之情形發生。 In the above step S460, one end of the hot-side strong exhaust pipe 90 is connected to the furnace chamber 102 of the direct-fired incinerator (TO) 10, and the other end of the hot-side strong exhaust pipe 90 is connected to the direct-fired incinerator (TO) 10. The outlet 12 of the type incinerator (TO) 10 is connected, wherein the hot side strong discharge line 9 The 0 series is provided with at least one damper 901, and two dampers (not shown) can also be provided in conjunction with the pipeline, so that the air volume of the hot-side strong exhaust pipeline 90 can be regulated through the damper 901. Therefore, When the concentration of volatile organic compounds (VOCs) becomes high, the air volume of the furnace chamber 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot-side strong exhaust line 90, and part of the incinerated high-temperature gas can be delivered To the outlet 12 of the direct-fired incinerator (TO) 10, the hot-side strong exhaust pipe 90 has the effect of adjusting the heat recovery amount or concentration, so that the organic waste gas can be prevented from being treated by the direct-fired incinerator (TO). TO)10 will not overheat due to too high furnace temperature, or even lead to shutdown.

由以上詳細說明,可使熟知本項技藝者明瞭本發明的確可達成前述目的,實已符合專利法之規定,爰提出發明專利申請。 From the above detailed description, it can be understood by those skilled in the art that the present invention can indeed achieve the aforesaid object, and it is in compliance with the provisions of the Patent Law, and an application for a patent for invention can be filed.

惟以上所述者,僅為本發明之較佳實施例而已,當不能以此限定本發明實施之範圍;故,凡依本發明申請專利範圍及發明說明書內容所作之簡單的等效變化與修飾,皆應仍屬本發明專利涵蓋之範圍內。 However, the above are only the preferred embodiments of the present invention, and should not limit the scope of the present invention; therefore, any simple equivalent changes and modifications made according to the scope of the patent application of the present invention and the contents of the description of the invention , shall still fall within the scope covered by the patent of the present invention.

10:直燃式焚燒爐(TO) 10: Direct-fired incinerator (TO)

101:爐頭 101: Stove

102:爐膛 102: Hearth

11:入口 11: Entrance

12:出口 12: Export

20:第一熱交換器 20: First heat exchanger

21:第一冷側管路 21: The first cold side pipeline

22:第一熱側管路 22: The first hot side pipeline

23:第一冷側輸送管路 23: The first cold side delivery pipeline

30:第二熱交換器 30: Second heat exchanger

31:第二冷側管路 31: Second cold side pipeline

32:第二熱側管路 32: Second hot side piping

60:吸附轉輪 60: Adsorption runner

601:吸附區 601: Adsorption zone

602:冷卻區 602: Cooling Zone

603:脫附區 603: Desorption zone

61:廢氣進氣管路 61: Exhaust gas intake line

62:淨氣排放管路 62: Clean air discharge pipeline

63:冷卻氣進氣管路 63: Cooling air intake line

64:冷卻氣輸送管路 64: Cooling gas delivery pipeline

65:熱氣輸送管路 65: Hot gas delivery pipeline

66:脫附濃縮氣體管路 66: Desorption concentrated gas pipeline

80:煙囪 80: Chimney

90:熱側強排管路 90: Hot side strong discharge pipeline

901:調節風門 901: Adjust the damper

Claims (16)

一種節能型單轉輪熱側旁通過溫控制系統,係包括: An energy-saving single runner hot side bypass temperature control system, comprising: 一直燃式焚燒爐(TO),該直燃式焚燒爐(TO)係設有一爐頭及一爐膛,該爐頭與該爐膛係相通,該直燃式焚燒爐(TO)係設有入口及出口,該入口係設於該爐頭處,該出口係設於該爐膛處; A direct-fired incinerator (TO), the direct-fired incinerator (TO) is provided with a burner head and a hearth, the burner head is communicated with the hearth, and the direct-fired incinerator (TO) is provided with an inlet and a hearth. an outlet, the inlet being provided at the burner head, and the outlet being provided at the hearth; 一第一熱交換器,該第一熱交換器係設於該直燃式焚燒爐(TO)內,該第一熱交換器係設有第一冷側管路及第一熱側管路; a first heat exchanger, the first heat exchanger is installed in the direct-fired incinerator (TO), and the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline; 一第二熱交換器,該第二熱交換器係設於該直燃式焚燒爐(TO)內,該第二熱交換器係設有第二冷側管路及第二熱側管路; a second heat exchanger, the second heat exchanger is installed in the direct-fired incinerator (TO), and the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline; 一第一冷側輸送管路,該第一冷側輸送管路的一端係與該第一冷側管路的另一端連接,該第一冷側輸送管路的另一端係與該直燃式焚燒爐(TO)之入口連接; A first cold-side conveying pipeline, one end of the first cold-side conveying pipeline is connected to the other end of the first cold-side pipeline, and the other end of the first cold-side conveying pipeline is connected to the direct-fired type The inlet connection of the incinerator (TO); 一吸附轉輪,該吸附轉輪係設有吸附區、冷卻區及脫附區,該吸附轉輪係連接有一廢氣進氣管路、一淨氣排放管路、一冷卻氣進氣管路、一冷卻氣輸送管路、一熱氣輸送管路及一脫附濃縮氣體管路,該廢氣進氣管路的一端係連接至該吸附轉輪之吸附區的一側,該淨氣排放管路的一端係與該吸附轉輪之吸附區的另一側連接,該冷卻氣進氣管路的一端係與該吸附轉輪之冷卻區之一側連接,該冷卻氣輸送管路的一端係與該吸附轉輪之冷卻區的另一側連接,該冷卻氣輸送管路的另一端係與該第二熱交換器之第二冷側管路的一端連接,該熱氣輸送管路的一端係與該吸附轉輪之脫附區的另一側連接,該熱氣輸送管路的另一端係與該第二熱交換器之第二冷側管路的另一端連接,該脫附濃縮氣體管路的一端係與該 吸附轉輪之脫附區的一側連接,該脫附濃縮氣體管路的另一端係與該第一熱交換器之第一冷側管路的一端連接; An adsorption runner. The adsorption runner system is provided with an adsorption area, a cooling area and a desorption area. The adsorption runner system is connected with an exhaust gas intake pipeline, a clean gas discharge pipeline, a cooling gas intake pipeline, A cooling gas delivery pipeline, a hot gas delivery pipeline and a desorption concentrated gas pipeline, one end of the exhaust gas inlet pipeline is connected to one side of the adsorption area of the adsorption runner, and the clean gas discharge pipeline has One end is connected with the other side of the adsorption area of the adsorption runner, one end of the cooling gas inlet pipeline is connected with one side of the cooling area of the adsorption runner, and one end of the cooling gas delivery pipeline is connected with the The other side of the cooling zone of the adsorption runner is connected, the other end of the cooling gas delivery pipeline is connected with one end of the second cold side pipeline of the second heat exchanger, and one end of the hot gas delivery pipeline is connected with the second cold side pipeline of the second heat exchanger. The other side of the desorption zone of the adsorption runner is connected, the other end of the hot gas conveying pipeline is connected with the other end of the second cold side pipeline of the second heat exchanger, and one end of the desorption concentrated gas pipeline is connected tied to the One side of the desorption zone of the adsorption runner is connected, and the other end of the desorption concentrated gas pipeline is connected with one end of the first cold side pipeline of the first heat exchanger; 一煙囪,該淨氣排放管路的另一端係與該煙囪連接;以及 a chimney to which the other end of the clean air discharge line is connected; and 一熱側強排管路,該熱側強排管路的一端係與該直燃式焚燒爐(TO)之爐膛連接,該熱側強排管路的另一端係與該第二熱交換器之第二熱側管路與該第一熱交換器之第一熱側管路之間相連處連接,該熱側強排管路係設有至少一調節風門。 A hot-side forced-exhaust pipeline, one end of the hot-side forced-discharge pipeline is connected to the furnace of the direct-fired incinerator (TO), and the other end of the hot-side forced-discharge pipeline is connected to the second heat exchanger The second hot-side pipeline is connected with the first hot-side pipeline of the first heat exchanger, and the hot-side strong discharge pipeline system is provided with at least one regulating damper. 一種節能型單轉輪熱側旁通過溫控制系統,係包括: An energy-saving single runner hot side bypass temperature control system, comprising: 一直燃式焚燒爐(TO),該直燃式焚燒爐(TO)係設有一爐頭及一爐膛,該爐頭與該爐膛係相通,該直燃式焚燒爐(TO)係設有入口及出口,該入口係設於該爐頭處,該出口係設於該爐膛處; A direct-fired incinerator (TO), the direct-fired incinerator (TO) is provided with a burner head and a hearth, the burner head is communicated with the hearth, and the direct-fired incinerator (TO) is provided with an inlet and a hearth. an outlet, the inlet being provided at the burner head, and the outlet being provided at the hearth; 一第一熱交換器,該第一熱交換器係設於該直燃式焚燒爐(TO)內,該第一熱交換器係設有第一冷側管路及第一熱側管路; a first heat exchanger, the first heat exchanger is installed in the direct-fired incinerator (TO), and the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline; 一第二熱交換器,該第二熱交換器係設於該直燃式焚燒爐(TO)內,該第二熱交換器係設有第二冷側管路及第二熱側管路; a second heat exchanger, the second heat exchanger is installed in the direct-fired incinerator (TO), and the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline; 一第一冷側輸送管路,該第一冷側輸送管路的一端係與該第一冷側管路的另一端連接,該第一冷側輸送管路的另一端係與該直燃式焚燒爐(TO)之入口連接; A first cold-side conveying pipeline, one end of the first cold-side conveying pipeline is connected to the other end of the first cold-side pipeline, and the other end of the first cold-side conveying pipeline is connected to the direct-fired type The inlet connection of the incinerator (TO); 一吸附轉輪,該吸附轉輪係設有吸附區、冷卻區及脫附區,該吸附轉輪係連接有一廢氣進氣管路、一淨氣排放管路、一冷卻氣進氣管路、一冷卻氣輸送管路、一熱氣輸送管路及一脫附濃縮氣體管路,該廢氣進氣管路的一端係連接至該吸附轉輪之吸附區的一側,該淨氣排放管路的一端 係與該吸附轉輪之吸附區的另一側連接,該冷卻氣進氣管路的一端係與該吸附轉輪之冷卻區之一側連接,該冷卻氣輸送管路的一端係與該吸附轉輪之冷卻區的另一側連接,該冷卻氣輸送管路的另一端係與該第二熱交換器之第二冷側管路的一端連接,該熱氣輸送管路的一端係與該吸附轉輪之脫附區的另一側連接,該熱氣輸送管路的另一端係與該第二熱交換器之第二冷側管路的另一端連接,該脫附濃縮氣體管路的一端係與該吸附轉輪之脫附區的一側連接,該脫附濃縮氣體管路的另一端係與該第一熱交換器之第一冷側管路的一端連接; An adsorption runner. The adsorption runner system is provided with an adsorption area, a cooling area and a desorption area. The adsorption runner system is connected with an exhaust gas intake pipeline, a clean gas discharge pipeline, a cooling gas intake pipeline, A cooling gas delivery pipeline, a hot gas delivery pipeline and a desorption concentrated gas pipeline, one end of the exhaust gas inlet pipeline is connected to one side of the adsorption area of the adsorption runner, and the clean gas discharge pipeline has one end It is connected to the other side of the adsorption zone of the adsorption wheel, one end of the cooling gas inlet pipeline is connected to one side of the cooling zone of the adsorption wheel, and one end of the cooling gas delivery pipeline is connected to the adsorption The other side of the cooling zone of the runner is connected, the other end of the cooling gas delivery pipeline is connected to one end of the second cold side pipeline of the second heat exchanger, and one end of the hot gas delivery pipeline is connected to the adsorption The other side of the desorption zone of the runner is connected, the other end of the hot gas conveying pipeline is connected with the other end of the second cold side pipeline of the second heat exchanger, and one end of the desorbed concentrated gas pipeline is connected is connected with one side of the desorption zone of the adsorption runner, and the other end of the desorption concentrated gas pipeline is connected with one end of the first cold side pipeline of the first heat exchanger; 一煙囪,該淨氣排放管路的另一端係與該煙囪連接;以及 a chimney to which the other end of the clean air discharge line is connected; and 一熱側強排管路,該熱側強排管路的一端係與該直燃式焚燒爐(TO)之爐膛連接,該熱側強排管路的另一端係與該直燃式焚燒爐(TO)之出口連接,該熱側強排管路係設有至少一調節風門。 A hot side strong discharge pipeline, one end of the hot side strong discharge pipeline is connected with the furnace of the direct-fired incinerator (TO), and the other end of the hot-side strong discharge pipeline is connected with the direct-fired incinerator The outlet of (TO) is connected, and the hot side strong exhaust pipe system is provided with at least one regulating damper. 如申請專利範圍第1或2項所述之節能型單轉輪熱側旁通過溫控制系統,其中該直燃式焚燒爐(TO)之出口係進一步連接至該煙囪。 The energy-saving single-rotor hot-side bypass temperature control system described in claim 1 or 2, wherein the outlet of the direct-fired incinerator (TO) is further connected to the chimney. 如申請專利範圍第1或2項所述之節能型單轉輪熱側旁通過溫控制系統,其中該冷卻氣進氣管路係進一步為供新鮮空氣或是外氣來進入。 According to the energy-saving single runner hot side bypass temperature control system as described in claim 1 or 2, the cooling air intake pipe system is further provided for fresh air or outside air to enter. 如申請專利範圍第1或2項所述之節能型單轉輪熱側旁通過溫控制系統,其中該廢氣進氣管路係進一步設有一廢氣連通管路,該廢氣連通管路係與該冷卻氣進氣管路連接,該廢氣連通管路係進一步設有一廢氣連通控制閥門,以控制該廢氣連通管路的風量。 According to the energy-saving single runner hot-side bypass temperature control system described in claim 1 or 2, the exhaust gas intake pipe system is further provided with an exhaust gas communication pipe, and the exhaust gas communication pipe system is connected with the cooling The exhaust gas communication pipeline is further provided with an exhaust gas communication control valve to control the air volume of the exhaust gas communication pipeline. 如申請專利範圍第1或2項所述之節能型單轉輪熱側旁通過溫控制系統,其中該脫附濃縮氣體管路係進一步設有一風機。 The energy-saving single-wheel hot-side bypass temperature control system described in claim 1 or 2, wherein the desorption and concentrated gas pipeline system is further provided with a fan. 如申請專利範圍第1或2項所述之節能型單轉輪熱側旁通過溫控制系統,其中該淨氣排放管路係進一步設有一風機。 The energy-saving single runner hot side bypass temperature control system as described in claim 1 or 2, wherein the clean air discharge line system is further provided with a fan. 一種節能型單轉輪熱側旁通過溫控制方法,主要係用於有機廢氣處理系統,且設有一直燃式焚燒爐(TO),一第一熱交換器、一第二熱交換器、一第一冷側輸送管路、一吸附轉輪及一煙囪,該直燃式焚燒爐(TO)係設有一爐頭及一爐膛,該爐頭與該爐膛係相通,該直燃式焚燒爐(TO)係設有入口及出口,該入口係設於該爐頭處,該出口係設於該爐膛處,該第一熱交換器係設有第一冷側管路及第一熱側管路,該第二熱交換器係設有第二冷側管路及第二熱側管路,第一冷側輸送管路的一端係與該第一冷側管路的另一端連接,該第一冷側輸送管路的另一端係與該直燃式焚燒爐(TO)之入口連接,該吸附轉輪係設有吸附區、冷卻區及脫附區,該吸附轉輪係連接有一廢氣進氣管路、一淨氣排放管路、一冷卻氣進氣管路、一冷卻氣輸送管路、一熱氣輸送管路及一脫附濃縮氣體管路,而該控制方法的主要步驟係包括: An energy-saving single-runner hot-side bypass temperature control method is mainly used in an organic waste gas treatment system, and is provided with a direct-fired incinerator (TO), a first heat exchanger, a second heat exchanger, a The first cold side conveying pipeline, an adsorption runner and a chimney, the direct-fired incinerator (TO) is provided with a burner and a furnace, the burner is communicated with the furnace, and the direct-fired incinerator ( TO) is provided with an inlet and an outlet, the inlet is set at the furnace head, the outlet is set at the furnace, and the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline , the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, one end of the first cold side delivery pipeline is connected with the other end of the first cold side pipeline, the first cold side pipeline The other end of the cold side conveying pipeline is connected to the inlet of the direct-fired incinerator (TO). The adsorption wheel train is provided with an adsorption zone, a cooling zone and a desorption zone. The adsorption wheel train is connected to an exhaust gas intake. pipeline, a clean gas discharge pipeline, a cooling gas intake pipeline, a cooling gas delivery pipeline, a hot gas delivery pipeline and a desorption concentrated gas pipeline, and the main steps of the control method include: 輸入待吸附之氣體:將廢氣透過該廢氣進氣管路的另一端來送入該吸附轉輪之吸附區的一側; Input the gas to be adsorbed: send the exhaust gas to one side of the adsorption zone of the adsorption runner through the other end of the exhaust gas inlet pipe; 吸附轉輪進行吸附:透過該吸附轉輪之吸附區進行吸附後,由該吸附轉輪之吸附區的另一側將吸附後之氣體透過該淨氣排放管路的另一端來輸出; Adsorption by adsorption wheel: after adsorption is carried out through the adsorption zone of the adsorption wheel, the gas after adsorption is output through the other end of the clean gas discharge pipeline from the other side of the adsorption zone of the adsorption wheel; 輸入冷卻氣體:透過該冷卻氣進氣管路的另一端來輸送冷卻氣至該吸附轉輪之冷卻區進行冷卻,再透過該冷卻氣輸送管路的另一端來將經過該吸附轉輪之冷卻區的冷卻氣輸送到該第二熱交換器之第二冷側管路的 一端; Input cooling gas: send cooling gas through the other end of the cooling gas inlet pipeline to the cooling area of the adsorption wheel for cooling, and then pass through the other end of the cooling gas delivery pipeline to cool the adsorption wheel The cooling gas from the zone is sent to the second cold side pipeline of the second heat exchanger. one end; 輸送熱氣脫附:透過與第二熱交換器之第二冷側管路的另一端所連接的熱氣輸送管路來將熱氣輸送到該吸附轉輪之脫附區進行脫附,再透過該脫附濃縮氣體管路的另一端來將脫附濃縮氣體輸送到第一熱交換器之第一冷側管路的一端; Transporting hot gas for desorption: through the hot gas transport pipeline connected to the other end of the second cold side pipeline of the second heat exchanger, the hot gas is transported to the desorption zone of the adsorption runner for desorption, and then passed through the desorption Attach the other end of the concentrated gas pipeline to deliver the desorbed concentrated gas to one end of the first cold side pipeline of the first heat exchanger; 脫附濃縮氣體輸送:該脫附濃縮氣體再透過該第一熱交換器之第一冷側管路的另一端所連接的第一冷側輸送管路來輸送到該直燃式焚燒爐(TO)之入口; Delivery of desorption concentrated gas: the desorption concentrated gas is then transported to the direct-fired incinerator (TO ) entrance; 焚燒後之氣體輸送:將該直燃式焚燒爐(TO)之爐頭所燃燒後而產生的焚燒後之氣體輸送到該第二熱交換器之第二熱側管路的一端,再由該第二熱交換器之第二熱側管路的另一端輸送到該第一熱交換器之第一熱側管路的一端,最後由該第一熱交換器之第一熱側管路的另一端輸送到該直燃式焚燒爐(TO)之出口;以及 Delivery of gas after incineration: The gas after combustion produced by the burner of the direct-fired incinerator (TO) is delivered to one end of the second hot-side pipeline of the second heat exchanger, and then sent to the end of the second hot side pipeline of the second heat exchanger. The other end of the second hot-side pipe of the second heat exchanger is transported to one end of the first hot-side pipe of the first heat exchanger, and finally sent to the other end of the first hot-side pipe of the first heat exchanger One end is delivered to the outlet of the direct-fired incinerator (TO); and 熱側強排管路調節:該直燃式焚燒爐(TO)之爐膛係設有一熱側強排管路,該熱側強排管路的一端係與該直燃式焚燒爐(TO)之爐膛連接,該熱側強排管路的另一端係與該第二熱交換器之第二熱側管路與該第一熱交換器之第一熱側管路之間相連處連接,該熱側強排管路係設有至少一調節風門,以透過該熱側強排管路來進行調節該直燃式焚燒爐(TO)之爐膛的風量。 Adjustment of hot-side forced discharge pipeline: The furnace of the direct-fired incinerator (TO) is provided with a hot-side forced-discharge pipeline, and one end of the hot-side forced-discharge pipeline is connected to the direct-fired incinerator (TO). The furnace is connected, and the other end of the hot-side strong discharge pipe is connected to the connection between the second hot-side pipe of the second heat exchanger and the first hot-side pipe of the first heat exchanger. The side strong exhaust pipe system is provided with at least one regulating damper to adjust the air volume of the furnace chamber of the direct-fired incinerator (TO) through the hot side strong exhaust pipe. 一種節能型單轉輪熱側旁通過溫控制方法,主要係用於有機廢氣處理系統,且設有一直燃式焚燒爐(TO),一第一熱交換器、一第二熱交換器、一第一冷側輸送管路、一吸附轉輪及一煙囪,該直燃式焚燒爐(TO)係設 有一爐頭及一爐膛,該爐頭與該爐膛係相通,該直燃式焚燒爐(TO)係設有入口及出口,該入口係設於該爐頭處,該出口係設於該爐膛處,該第一熱交換器係設有第一冷側管路及第一熱側管路,該第二熱交換器係設有第二冷側管路及第二熱側管路,第一冷側輸送管路的一端係與該第一冷側管路的另一端連接,該第一冷側輸送管路的另一端係與該直燃式焚燒爐(TO)之入口連接,該吸附轉輪係設有吸附區、冷卻區及脫附區,該吸附轉輪係連接有一廢氣進氣管路、一淨氣排放管路、一冷卻氣進氣管路、一冷卻氣輸送管路、一熱氣輸送管路及一脫附濃縮氣體管路,而該控制方法的主要步驟係包括: An energy-saving single-runner hot-side bypass temperature control method is mainly used in an organic waste gas treatment system, and is provided with a direct-fired incinerator (TO), a first heat exchanger, a second heat exchanger, a The first cold side conveying pipeline, an adsorption runner and a chimney, the direct-fired incinerator (TO) is equipped with There is a burner head and a hearth, the burner head is communicated with the hearth, the direct-fired incinerator (TO) is provided with an inlet and an outlet, the inlet is arranged at the burner head, and the outlet is arranged at the hearth , the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline, the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, the first cold side pipeline One end of the side conveying pipeline is connected with the other end of the first cold side pipeline, and the other end of the first cold side conveying pipeline is connected with the inlet of the direct-fired incinerator (TO). The adsorption runner The system is provided with an adsorption zone, a cooling zone and a desorption zone. The adsorption runner is connected with an exhaust gas intake pipeline, a clean air discharge pipeline, a cooling gas intake pipeline, a cooling gas delivery pipeline, and a hot gas pipeline. The conveying pipeline and a desorption concentrated gas pipeline, and the main steps of the control method include: 輸入待吸附之氣體:將廢氣透過該廢氣進氣管路的另一端來送入該吸附轉輪之吸附區的一側; Input the gas to be adsorbed: send the exhaust gas to one side of the adsorption zone of the adsorption runner through the other end of the exhaust gas inlet pipe; 吸附轉輪進行吸附:透過該吸附轉輪之吸附區進行吸附後,由該吸附轉輪之吸附區的另一側將吸附後之氣體透過該淨氣排放管路的另一端來輸出; Adsorption by adsorption wheel: after adsorption is carried out through the adsorption zone of the adsorption wheel, the gas after adsorption is output through the other end of the clean gas discharge pipeline from the other side of the adsorption zone of the adsorption wheel; 輸入冷卻氣體:透過該冷卻氣進氣管路的另一端來輸送冷卻氣至該吸附轉輪之冷卻區進行冷卻,再透過該冷卻氣輸送管路的另一端來將經過該吸附轉輪之冷卻區的冷卻氣輸送到該第二熱交換器之第二冷側管路的一端; Input cooling gas: send cooling gas through the other end of the cooling gas inlet pipeline to the cooling area of the adsorption wheel for cooling, and then pass through the other end of the cooling gas delivery pipeline to cool the adsorption wheel The cooling gas of the zone is delivered to one end of the second cold side pipeline of the second heat exchanger; 輸送熱氣脫附:透過與第二熱交換器之第二冷側管路的另一端所連接的熱氣輸送管路來將熱氣輸送到該吸附轉輪之脫附區進行脫附,再透過該脫附濃縮氣體管路的另一端來將脫附濃縮氣體輸送到第一熱交換器之第一冷側管路的一端; Transporting hot gas for desorption: through the hot gas transport pipeline connected to the other end of the second cold side pipeline of the second heat exchanger, the hot gas is transported to the desorption zone of the adsorption runner for desorption, and then passed through the desorption Attach the other end of the concentrated gas pipeline to deliver the desorbed concentrated gas to one end of the first cold side pipeline of the first heat exchanger; 脫附濃縮氣體輸送:該脫附濃縮氣體再透過該第一熱交換器之第一冷側管路的另一端所連接的第一冷側輸送管路來輸送到該直燃式焚燒爐(TO)之入口; Delivery of desorption concentrated gas: the desorption concentrated gas is then transported to the direct-fired incinerator (TO ) entrance; 焚燒後之氣體輸送:將該直燃式焚燒爐(TO)之爐頭所燃燒後而產生的焚燒後之氣體輸送到該第二熱交換器之第二熱側管路的一端,再由該第二熱交換器之第二熱側管路的另一端輸送到該第一熱交換器之第一熱側管路的一端,最後由該第一熱交換器之第一熱側管路的另一端輸送到該直燃式焚燒爐(TO)之出口;以及 Delivery of gas after incineration: The gas after combustion produced by the burner of the direct-fired incinerator (TO) is delivered to one end of the second hot-side pipeline of the second heat exchanger, and then sent to the end of the second hot side pipeline of the second heat exchanger. The other end of the second hot-side pipe of the second heat exchanger is transported to one end of the first hot-side pipe of the first heat exchanger, and finally sent to the other end of the first hot-side pipe of the first heat exchanger One end is delivered to the outlet of the direct-fired incinerator (TO); and 熱側強排管路調節:該直燃式焚燒爐(TO)之爐膛係設有一熱側強排管路,該熱側強排管路的一端係與該直燃式焚燒爐(TO)之爐膛連接,該熱側強排管路的另一端係與該直燃式焚燒爐(TO)之出口連接,該熱側強排管路係設有至少一調節風門,以透過該熱側強排管路來進行調節該直燃式焚燒爐(TO)之爐膛的風量。 Adjustment of hot-side forced discharge pipeline: The furnace of the direct-fired incinerator (TO) is provided with a hot-side forced-discharge pipeline, and one end of the hot-side forced-discharge pipeline is connected to the direct-fired incinerator (TO). The furnace is connected, and the other end of the hot-side forced exhaust pipe is connected to the outlet of the direct-fired incinerator (TO). A pipeline is used to adjust the air volume of the furnace chamber of the direct-fired incinerator (TO). 一種節能型單轉輪熱側旁通過溫控制方法,主要係用於有機廢氣處理系統,且設有一直燃式焚燒爐(TO),一第一熱交換器、一第二熱交換器、一第一冷側輸送管路、一吸附轉輪及一煙囪,該直燃式焚燒爐(TO)係設有一爐頭及一爐膛,該爐頭與該爐膛係相通,該直燃式焚燒爐(TO)係設有入口及出口,該入口係設於該爐頭處,該出口係設於該爐膛處,該第一熱交換器係設有第一冷側管路及第一熱側管路,該第二熱交換器係設有第二冷側管路及第二熱側管路,第一冷側輸送管路的一端係與該第一冷側管路的另一端連接,該第一冷側輸送管路的另一端係與該直燃式焚燒爐(TO)之入口連接,該吸附轉輪係設有吸附區、冷卻區及脫附 區,該吸附轉輪係連接有一廢氣進氣管路、一淨氣排放管路、一冷卻氣進氣管路、一冷卻氣輸送管路、一熱氣輸送管路及一脫附濃縮氣體管路,而該控制方法的主要步驟係包括: An energy-saving single-runner hot-side bypass temperature control method is mainly used in an organic waste gas treatment system, and is provided with a direct-fired incinerator (TO), a first heat exchanger, a second heat exchanger, a The first cold side conveying pipeline, an adsorption runner and a chimney, the direct-fired incinerator (TO) is provided with a burner and a furnace, the burner is communicated with the furnace, and the direct-fired incinerator ( TO) is provided with an inlet and an outlet, the inlet is set at the furnace head, the outlet is set at the furnace, and the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline , the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, one end of the first cold side delivery pipeline is connected with the other end of the first cold side pipeline, the first cold side pipeline The other end of the cold side conveying pipeline is connected to the inlet of the direct-fired incinerator (TO), and the adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone The adsorption runner is connected with an exhaust gas intake pipeline, a clean gas discharge pipeline, a cooling gas intake pipeline, a cooling gas delivery pipeline, a hot gas delivery pipeline and a desorption concentrated gas pipeline , and the main steps of the control method include: 輸入待吸附之氣體:將廢氣透過該廢氣進氣管路的另一端來送入該吸附轉輪之吸附區的一側; Input the gas to be adsorbed: send the exhaust gas to one side of the adsorption zone of the adsorption runner through the other end of the exhaust gas inlet pipe; 吸附轉輪進行吸附:透過該吸附轉輪之吸附區進行吸附後,由該吸附轉輪之吸附區的另一側將吸附後之氣體透過該淨氣排放管路的另一端來輸出; Adsorption by adsorption wheel: after adsorption is carried out through the adsorption zone of the adsorption wheel, the gas after adsorption is output through the other end of the clean gas discharge pipeline from the other side of the adsorption zone of the adsorption wheel; 輸入冷卻氣體:透過該冷卻氣進氣管路的另一端來輸送冷卻氣至該吸附轉輪之冷卻區進行冷卻,再透過該冷卻氣輸送管路的另一端來將經過該吸附轉輪之冷卻區的冷卻氣輸送到該第二熱交換器之第二冷側管路的一端; Input cooling gas: send cooling gas through the other end of the cooling gas inlet pipeline to the cooling area of the adsorption wheel for cooling, and then pass through the other end of the cooling gas delivery pipeline to cool the adsorption wheel The cooling gas of the zone is delivered to one end of the second cold side pipeline of the second heat exchanger; 輸送熱氣脫附:透過與第二熱交換器之第二冷側管路的另一端所連接的熱氣輸送管路來將熱氣輸送到該吸附轉輪之脫附區進行脫附,再透過該脫附濃縮氣體管路的另一端來將脫附濃縮氣體輸送到第一熱交換器之第一冷側管路的一端; Transporting hot gas for desorption: through the hot gas transport pipeline connected to the other end of the second cold side pipeline of the second heat exchanger, the hot gas is transported to the desorption zone of the adsorption runner for desorption, and then passed through the desorption Attach the other end of the concentrated gas pipeline to deliver the desorbed concentrated gas to one end of the first cold side pipeline of the first heat exchanger; 脫附濃縮氣體輸送:該脫附濃縮氣體再透過該第一熱交換器之第一冷側管路的另一端所連接的第一冷側輸送管路來輸送到該直燃式焚燒爐(TO)之入口; Delivery of desorption concentrated gas: the desorption concentrated gas is then transported to the direct-fired incinerator (TO ) entrance; 焚燒後之氣體輸送:將該直燃式焚燒爐(TO)之爐頭所燃燒後而產生的焚燒後之氣體輸送到該第一熱交換器之第一熱側管路的一端,而由該第一熱交換器之第一熱側管路的另一端輸送到該第二熱交換器之第二熱側 管路的一端,再由該第二熱交換器之第二熱側管路的另一端輸送到該直燃式焚燒爐(TO)之出口;以及 Delivery of gas after incineration: The gas after combustion generated by the burner of the direct-fired incinerator (TO) is delivered to one end of the first hot side pipeline of the first heat exchanger, and the The other end of the first hot side pipeline of the first heat exchanger is sent to the second hot side of the second heat exchanger One end of the pipeline is transported from the other end of the second hot side pipeline of the second heat exchanger to the outlet of the direct-fired incinerator (TO); and 熱側強排管路調節:該直燃式焚燒爐(TO)之爐膛係設有一熱側強排管路,該熱側強排管路的一端係與該直燃式焚燒爐(TO)之爐膛連接,該熱側強排管路的另一端係與該第一熱交換器之第一熱側管路與該第二熱交換器之第二熱側管路之間相連處連接,該熱側強排管路係設有至少一調節風門,以透過該熱側強排管路來進行調節該直燃式焚燒爐(TO)之爐膛的風量。 Adjustment of hot-side forced discharge pipeline: The furnace of the direct-fired incinerator (TO) is provided with a hot-side forced-discharge pipeline, and one end of the hot-side forced-discharge pipeline is connected to the direct-fired incinerator (TO). The furnace is connected, and the other end of the hot-side strong discharge pipe is connected to the connection between the first hot-side pipe of the first heat exchanger and the second hot-side pipe of the second heat exchanger. The side strong exhaust pipe system is provided with at least one regulating damper to adjust the air volume of the furnace chamber of the direct-fired incinerator (TO) through the hot side strong exhaust pipe. 一種節能型單轉輪熱側旁通過溫控制方法,主要係用於有機廢氣處理系統,且設有一直燃式焚燒爐(TO),一第一熱交換器、一第二熱交換器、一第一冷側輸送管路、一吸附轉輪及一煙囪,該直燃式焚燒爐(TO)係設有一爐頭及一爐膛,該爐頭與該爐膛係相通,該直燃式焚燒爐(TO)係設有入口及出口,該入口係設於該爐頭處,該出口係設於該爐膛處,該第一熱交換器係設有第一冷側管路及第一熱側管路,該第二熱交換器係設有第二冷側管路及第二熱側管路,第一冷側輸送管路的一端係與該第一冷側管路的另一端連接,該第一冷側輸送管路的另一端係與該直燃式焚燒爐(TO)之入口連接,該吸附轉輪係設有吸附區、冷卻區及脫附區,該吸附轉輪係連接有一廢氣進氣管路、一淨氣排放管路、一冷卻氣進氣管路、一冷卻氣輸送管路、一熱氣輸送管路及一脫附濃縮氣體管路,而該控制方法的主要步驟係包括: An energy-saving single-runner hot-side bypass temperature control method is mainly used in an organic waste gas treatment system, and is provided with a direct-fired incinerator (TO), a first heat exchanger, a second heat exchanger, a The first cold side conveying pipeline, an adsorption runner and a chimney, the direct-fired incinerator (TO) is provided with a burner and a furnace, the burner is communicated with the furnace, and the direct-fired incinerator ( TO) is provided with an inlet and an outlet, the inlet is set at the furnace head, the outlet is set at the furnace, and the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline , the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, one end of the first cold side delivery pipeline is connected with the other end of the first cold side pipeline, the first cold side pipeline The other end of the cold side conveying pipeline is connected to the inlet of the direct-fired incinerator (TO). The adsorption wheel train is provided with an adsorption zone, a cooling zone and a desorption zone. The adsorption wheel train is connected to an exhaust gas intake. pipeline, a clean gas discharge pipeline, a cooling gas intake pipeline, a cooling gas delivery pipeline, a hot gas delivery pipeline and a desorption concentrated gas pipeline, and the main steps of the control method include: 輸入待吸附之氣體:將廢氣透過該廢氣進氣管路的另一端來送入該吸附轉輪之吸附區的一側; Input the gas to be adsorbed: send the exhaust gas to one side of the adsorption zone of the adsorption runner through the other end of the exhaust gas inlet pipe; 吸附轉輪進行吸附:透過該吸附轉輪之吸附區進行吸附後,由該吸附轉輪之吸附區的另一側將吸附後之氣體透過該淨氣排放管路的另一端來輸出; Adsorption by adsorption wheel: after adsorption is carried out through the adsorption zone of the adsorption wheel, the gas after adsorption is output through the other end of the clean gas discharge pipeline from the other side of the adsorption zone of the adsorption wheel; 輸入冷卻氣體:透過該冷卻氣進氣管路的另一端來輸送冷卻氣至該吸附轉輪之冷卻區進行冷卻,再透過該冷卻氣輸送管路的另一端來將經過該吸附轉輪之冷卻區的冷卻氣輸送到該第二熱交換器之第二冷側管路的一端; Input cooling gas: send cooling gas through the other end of the cooling gas inlet pipeline to the cooling area of the adsorption wheel for cooling, and then pass through the other end of the cooling gas delivery pipeline to cool the adsorption wheel The cooling gas of the zone is delivered to one end of the second cold side pipeline of the second heat exchanger; 輸送熱氣脫附:透過與第二熱交換器之第二冷側管路的另一端所連接的熱氣輸送管路來將熱氣輸送到該吸附轉輪之脫附區進行脫附,再透過該脫附濃縮氣體管路的另一端來將脫附濃縮氣體輸送到第一熱交換器之第一冷側管路的一端; Transporting hot gas for desorption: through the hot gas transport pipeline connected to the other end of the second cold side pipeline of the second heat exchanger, the hot gas is transported to the desorption zone of the adsorption runner for desorption, and then passed through the desorption Attach the other end of the concentrated gas pipeline to deliver the desorbed concentrated gas to one end of the first cold side pipeline of the first heat exchanger; 脫附濃縮氣體輸送:該脫附濃縮氣體再透過該第一熱交換器之第一冷側管路的另一端所連接的第一冷側輸送管路來輸送到該直燃式焚燒爐(TO)之入口; Delivery of desorption concentrated gas: the desorption concentrated gas is then transported to the direct-fired incinerator (TO ) entrance; 焚燒後之氣體輸送:將該直燃式焚燒爐(TO)之爐頭所燃燒後而產生的焚燒後之氣體輸送到該第一熱交換器之第一熱側管路的一端,而由該第一熱交換器之第一熱側管路的另一端輸送到該第二熱交換器之第二熱側管路的一端,再由該第二熱交換器之第二熱側管路的另一端輸送到該直燃式焚燒爐(TO)之出口;以及 Delivery of gas after incineration: The gas after combustion generated by the burner of the direct-fired incinerator (TO) is delivered to one end of the first hot side pipeline of the first heat exchanger, and the The other end of the first hot side pipe of the first heat exchanger is transported to one end of the second hot side pipe of the second heat exchanger, and then sent to the other end of the second hot side pipe of the second heat exchanger. One end is delivered to the outlet of the direct-fired incinerator (TO); and 熱側強排管路調節:該直燃式焚燒爐(TO)之爐膛係設有一熱側強排管路,該熱側強排管路的一端係與該直燃式焚燒爐(TO)之爐膛連接,該熱側強排管路的另一端係與該直燃式焚燒爐(TO)之出口連接,該熱側強排 管路係設有至少一調節風門,以透過該熱側強排管路來進行調節該直燃式焚燒爐(TO)之爐膛的風量。 Adjustment of hot-side forced discharge pipeline: The furnace of the direct-fired incinerator (TO) is provided with a hot-side forced-discharge pipeline, and one end of the hot-side forced-discharge pipeline is connected to the direct-fired incinerator (TO). The furnace is connected, and the other end of the hot side strong discharge pipeline is connected with the outlet of the direct-fired incinerator (TO). The pipeline system is provided with at least one regulating damper, so as to adjust the air volume of the furnace chamber of the direct-fired incinerator (TO) through the hot-side strong exhaust pipeline. 如申請專利範圍第8、9、10或11項所述之節能型單轉輪熱側旁通過溫控制方法,其中該直燃式焚燒爐(TO)之出口係進一步連接至該煙囪。 The energy-saving single-rotor hot-side bypass temperature control method described in claim 8, 9, 10 or 11, wherein the outlet of the direct-fired incinerator (TO) is further connected to the chimney. 如申請專利範圍第8、9、10或11項所述之節能型單轉輪熱側旁通過溫控制方法,其中該冷卻氣進氣管路係進一步為供新鮮空氣或是外氣來進入。 According to the energy-saving single runner hot side bypass temperature control method described in claim 8, 9, 10 or 11, the cooling air intake pipe system is further provided for fresh air or outside air to enter. 如申請專利範圍第8、9、10或11項所述之節能型單轉輪熱側旁通過溫控制方法,其中該廢氣進氣管路係進一步設有一廢氣連通管路,該廢氣連通管路係與該冷卻氣進氣管路連接,該廢氣連通管路係進一步設有一廢氣連通控制閥門,以控制該廢氣連通管路的風量。 According to the energy-saving single runner hot side bypass temperature control method described in item 8, 9, 10 or 11 of the scope of application, wherein the exhaust gas intake pipe system is further provided with an exhaust gas communication pipe, and the exhaust gas communication pipe It is connected with the cooling gas intake pipeline, and the exhaust gas communication pipeline is further provided with an exhaust gas communication control valve to control the air volume of the exhaust gas communication pipeline. 如申請專利範圍第8、9、10或11項所述之節能型單轉輪熱側旁通過溫控制方法,其中該脫附濃縮氣體管路係進一步設有一風機。 The energy-saving single runner hot-side bypass temperature control method described in claim 8, 9, 10 or 11, wherein the desorption concentrated gas pipeline system is further provided with a fan. 如申請專利範圍第8、9、10或11項所述之節能型單轉輪熱側旁通過溫控制方法,其中該淨氣排放管路係進一步設有一風機。 According to the energy-saving single-runner hot-side bypass temperature control method described in item 8, 9, 10 or 11 of the patent application scope, the clean air discharge pipeline system is further provided with a fan.
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CN117685581A (en) * 2024-02-02 2024-03-12 陕西宝昱科技工业股份有限公司 Organic waste gas burns device
CN117685581B (en) * 2024-02-02 2024-05-10 陕西宝昱科技工业股份有限公司 Organic waste gas burns device

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