TWI714201B - Catalyst refluxing high-efficiency organic waste gas treatment system and method - Google Patents

Catalyst refluxing high-efficiency organic waste gas treatment system and method Download PDF

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TWI714201B
TWI714201B TW108128017A TW108128017A TWI714201B TW I714201 B TWI714201 B TW I714201B TW 108128017 A TW108128017 A TW 108128017A TW 108128017 A TW108128017 A TW 108128017A TW I714201 B TWI714201 B TW I714201B
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pipeline
gas
adsorption
cooling
heater
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TW108128017A
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TW202106369A (en
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鄭石治
扶亞民
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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 TW108128017A priority Critical patent/TWI714201B/en
Priority to CN201910951807.6A priority patent/CN112337296B/en
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation 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
    • B01D53/02—Separation 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
    • B01D53/06—Separation 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
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/38—Removing components of undefined structure
    • B01D53/44—Organic components
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/81—Solid phase processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86—Catalytic processes
    • B01D53/8678—Removing components of undefined structure
    • B01D53/8687—Organic components

Abstract

本發明為一種觸媒回流高效率有機廢氣處理系統及其方法，主要係將由該吸附轉輪之脫附區所排出的脫附濃縮氣體透過該吸附反應床將含矽的化合物反應成為二氧化矽(SiO2)並吸附，再進入該觸媒床進行處理後，再將經過該觸媒床處理之氣體進行熱回收，以及將經過該觸媒床處理之氣體導回至該吸附轉輪之廢氣進氣管路，使經過該觸媒床處理之氣體進入該吸附轉輪之吸附區循環利用，而不經過該煙囪來進行排放，讓該煙囪的排放量降低，並使有機廢氣的處理效率提升。 The present invention is a catalyst refluxing high-efficiency organic waste gas treatment system and method, which mainly pass the desorption concentrated gas discharged from the desorption zone of the adsorption rotor through the adsorption reaction bed to react silicon-containing compounds into silicon dioxide (SiO 2 ) and adsorb, and then enter the catalyst bed for treatment, then heat recovery of the gas treated by the catalyst bed, and return the gas treated by the catalyst bed to the exhaust gas of the adsorption rotor The gas inlet pipeline allows the gas processed by the catalyst bed to enter the adsorption zone of the adsorption runner for recycling without passing through the chimney for discharge, reducing the chimney emissions and improving the efficiency of organic waste gas treatment .

Description

觸媒回流高效率有機廢氣處理系統及其方法 Catalyst refluxing high-efficiency organic waste gas treatment system and method

本發明係有關於一種觸媒回流高效率有機廢氣處理系統及其方法，尤指一種用來將經過該觸媒床處理之氣體進入該吸附轉輪之吸附區循環利用，而不經過該煙囪來進行排放，讓該煙囪的排放量降低，並使有機廢氣的處理效率提升，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 a catalyst refluxing high-efficiency organic waste gas treatment system and method thereof, in particular to a method for recycling the gas processed by the catalyst bed into the adsorption zone of the adsorption runner without passing through the chimney. Discharge, reduce the emission of the chimney, and improve the efficiency of organic waste gas treatment, which is suitable for organic waste gas treatment systems or similar equipment in the semiconductor industry, optoelectronic industry or chemical-related industries.

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 the current manufacturing process in the semiconductor industry or the optoelectronic industry, volatile organic gases (VOC) are generated. Therefore, processing equipment for processing volatile organic gases (VOC) will be installed in each plant to avoid volatile organic gases. (VOC) is directly discharged into the air to cause air pollution. At present, most of the concentrated gas desorbed by the processing equipment is transported to the incinerator for combustion, and then the combusted 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懸浮微粒(PM10)及細懸浮微粒(PM2.5)空氣品質標準，並依據其國內健康影響研究結果，以健康影響為優先考量，將「細懸浮微粒(PM2.5)」24小時值訂為35μg/m3、年平均值訂為15μg/m3。且環保署初步訂於民國109(2020)年達成全國細懸浮微粒濃度年平均值15μg/m3的目標，同時將依國際管制趨勢發展，逐期檢討其細懸浮微粒(PM2.5)空氣品質標準，並朝達成WHO提出之空氣品質準則 值(24小時值訂為25μg/m3、年平均值訂為10μg/m3)為空氣品質改善目標。 However, in recent years, both the central government and local governments have attached great importance to air pollution. Therefore, air quality standards for suspended particulates (PM 10 ) and fine suspended particulates (PM 2.5 ) have been set in the emission standards of chimneys. And based on the results of its domestic health impact research, with health impact as the priority consideration, the 24-hour value of "fine suspended particulates (PM 2.5 )" is set at 35μg/m 3 and the annual average value is set at 15μg/m 3 . In addition, the Environmental Protection Agency preliminarily plans to achieve the national average concentration of fine suspended particulates of 15μg/m 3 in 109 (2020). At the same time, it will review its fine suspended particulates (PM 2.5 ) air quality standards in accordance with the development of international control trends. , And to achieve the air quality guidelines proposed by the WHO (the 24-hour value is set at 25μg/m 3 and the annual average is set at 10μg/m 3 ) as the air quality improvement target.

因此，本發明人有鑑於上述缺失，期提出一種具有提升有機廢氣處理效率的觸媒回流高效率有機廢氣處理系統及其方法，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-mentioned deficiencies, the present inventors hope to propose a catalyst recirculation high-efficiency organic waste gas treatment system and method that can improve the efficiency of organic waste gas treatment, so that users can easily operate and assemble, and are dedicated to research and design. In order to provide user convenience, it is the motive of the invention that the inventor wants to develop.

本發明之主要目的，在於提供一種觸媒回流高效率有機廢氣處理系統及其方法，主要係將由該吸附轉輪之脫附區所排出的脫附濃縮氣體透過該吸附反應床將含矽的化合物反應成為二氧化矽(SiO2)並吸附，再進入該觸媒床進行處理後，再將經過該觸媒床處理之氣體進行熱回收，以及將經過該觸媒床處理之氣體導回至該吸附轉輪之廢氣進氣管路，使經過該觸媒床處理之氣體進入該吸附轉輪之吸附區循環利用，而不經過該煙囪來進行排放，讓該煙囪的排放量降低，並使有機廢氣的處理效率提升，進而增加整體之實用性。 The main purpose of the present invention is to provide a catalyst recirculation high-efficiency organic waste gas treatment system and method thereof, mainly by passing the desorption concentrated gas discharged from the desorption zone of the adsorption rotor through the adsorption reaction bed to remove silicon-containing compounds It reacts to become silicon dioxide (SiO 2 ) and adsorbs, and then enters the catalyst bed for treatment, and then heats the gas treated by the catalyst bed to heat recovery, and returns the gas treated by the catalyst bed to the The exhaust gas inlet pipeline of the adsorption runner allows the gas processed by the catalyst bed to enter the adsorption zone of the adsorption runner for recycling, instead of passing through the chimney for discharge, reducing the emission of the chimney and making organic The efficiency of waste gas treatment is improved, thereby increasing the overall practicality.

本發明之另一目的，在於提供一種觸媒回流高效率有機廢氣處理系統及其方法，且透過該觸媒床處理之氣體先經由該第一熱交換器進行熱交換後再輸送到該第二熱交換器來進行熱交換，並經過一除塵設備或是一濾網裝置來進行粉塵的過濾，讓該觸媒床處理之氣體除了導回該吸附轉輪之廢氣進氣管路外，也用來提供給該第一熱交換器及該第二熱交換器進行熱交換，以具有節省能源之效能，進而增加整體之使用性。 Another object of the present invention is to provide a catalyst recirculation high-efficiency organic waste gas treatment system and method, and the gas processed through the catalyst bed is first exchanged through the first heat exchanger and then sent to the second The heat exchanger is used for heat exchange, and through a dust removal device or a filter device to filter the dust, so that the gas processed by the catalyst bed is not only returned to the exhaust gas inlet pipe of the adsorption rotor, but also used To provide the first heat exchanger and the second heat exchanger for heat exchange, so as to save energy and increase the overall usability.

本發明之再一目的，在於提供一種觸媒回流高效率有機廢氣處理系統及其方法，且透過該觸媒床處理之氣體先經由該冷卻器進行高溫 熱氣的降溫後再輸送到該第二熱交換器來進行熱交換，並經過一除塵設備或是一濾網裝置來進行粉塵的過濾，讓該觸媒床處理之氣體除了導回該吸附轉輪之廢氣進氣管路外，也用來提供給該第二熱交換器進行熱交換，以具有節省能源之效能，進而增加整體之便利性。 Another object of the present invention is to provide a catalyst recirculation high-efficiency organic waste gas treatment system and method thereof, and the gas processed through the catalyst bed is first subjected to high temperature through the cooler After cooling, the hot gas is sent to the second heat exchanger for heat exchange, and is filtered through a dust removal device or a filter device, so that the gas processed by the catalyst bed is returned to the adsorption rotor The exhaust gas inlet pipe is also used to provide the second heat exchanger for heat exchange, so as to save energy and increase the overall convenience.

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 and drawings of the present invention. However, the accompanying drawings are only for reference and description, and are not intended to limit the present invention.

10‧‧‧觸媒床 10‧‧‧Catalyst bed

11‧‧‧進氣口 11‧‧‧Air inlet

12‧‧‧出氣口 12‧‧‧Exhaust port

20‧‧‧吸附反應床 20‧‧‧Adsorption reaction bed

21‧‧‧吸附反應床輸送管路 21‧‧‧Adsorption reaction bed transport pipeline

30‧‧‧第一加熱器 30‧‧‧First heater

31‧‧‧第一加熱氣輸送管路 31‧‧‧The first heating gas delivery pipeline

40‧‧‧吸附轉輪 40‧‧‧Adsorption wheel

401‧‧‧吸附區 401‧‧‧Adsorption zone

402‧‧‧冷卻區 402‧‧‧Cooling area

403‧‧‧脫附區 403‧‧‧Desorption area

41‧‧‧廢氣進氣管路 41‧‧‧Exhaust gas intake pipe

42‧‧‧淨氣排放管路 42‧‧‧Clean air discharge pipeline

421‧‧‧風車 421‧‧‧Windmill

43‧‧‧冷卻氣進氣管路 43‧‧‧Cooling gas intake pipe

431‧‧‧氣體旁通管路 431‧‧‧Gas bypass line

44‧‧‧冷卻氣輸送管路 44‧‧‧Cooling gas delivery pipeline

441‧‧‧冷卻氣控制閥門 441‧‧‧Cooling gas control valve

45‧‧‧熱氣輸送管路 45‧‧‧Hot gas delivery pipeline

451‧‧‧熱氣控制閥門 451‧‧‧Hot gas control valve

46‧‧‧脫附濃縮氣體管路 46‧‧‧Desorption concentrated gas pipeline

461‧‧‧風車 461‧‧‧Windmill

47‧‧‧連通管路 47‧‧‧Connecting pipeline

471‧‧‧連通控制閥門 471‧‧‧Connecting control valve

50‧‧‧第二加熱器 50‧‧‧Second heater

60‧‧‧第一熱交換器 60‧‧‧The first heat exchanger

601‧‧‧第一冷側管路 601‧‧‧The first cold side pipeline

602‧‧‧第一熱側管路 602‧‧‧The first hot side pipeline

61‧‧‧第一熱氣回收管路 61‧‧‧The first hot gas recovery pipeline

62‧‧‧第一觸媒床熱氣回收管路 62‧‧‧The first catalyst bed hot gas recovery pipeline

63‧‧‧第一脫附濃縮氣體輸送管路 63‧‧‧The first desorption concentrated gas delivery pipeline

70‧‧‧第二熱交換器 70‧‧‧Second heat exchanger

701‧‧‧第二冷側管路 701‧‧‧Second cold side pipeline

702‧‧‧第二熱側管路 702‧‧‧Second hot side pipeline

71‧‧‧第二脫附濃縮氣體輸送管路 71‧‧‧Second desorption concentrated gas delivery pipeline

72‧‧‧第二熱氣回收管路 72‧‧‧Second hot gas recovery pipeline

721‧‧‧除塵設備 721‧‧‧Dust removal equipment

722‧‧‧濾網裝置 722‧‧‧Filter device

80‧‧‧冷卻器 80‧‧‧Cooler

801‧‧‧冷卻水管路 801‧‧‧Cooling water pipeline

81‧‧‧冷卻熱氣回收管路 81‧‧‧Cooling hot gas recovery pipeline

82‧‧‧觸媒床熱氣回收管路 82‧‧‧Catalyst bed hot gas recovery pipeline

90‧‧‧煙囪 90‧‧‧Chimney

S100‧‧‧吸附區吸附 S100‧‧‧Adsorption zone adsorption

S110‧‧‧冷卻區冷卻 S110‧‧‧Cooling area cooling

S120‧‧‧脫附區脫附 S120‧‧‧Desorption zone desorption

S130‧‧‧脫附濃縮氣體輸送 S130‧‧‧Desorption concentrated gas delivery

S140‧‧‧吸附反應床吸附 S140‧‧‧Adsorption reaction bed adsorption

S150‧‧‧觸媒床處理 S150‧‧‧Catalyst bed treatment

S160‧‧‧觸媒床氣體輸送 S160‧‧‧Catalyst bed gas delivery

S170‧‧‧觸媒床氣體回收輸送 S170‧‧‧Catalyst bed gas recovery and transportation

S200‧‧‧吸附區吸附 S200‧‧‧Adsorption zone adsorption

S210‧‧‧冷卻區冷卻 S210‧‧‧Cooling zone cooling

S220‧‧‧脫附區脫附 S220‧‧‧Desorption zone desorption

S230‧‧‧脫附濃縮氣體輸送 S230‧‧‧Desorption concentrated gas delivery

S240‧‧‧吸附反應床吸附 S240‧‧‧Adsorption reaction bed adsorption

S250‧‧‧觸媒床處理 S250‧‧‧Catalyst bed treatment

S260‧‧‧觸媒床氣體輸送 S260‧‧‧Catalyst bed gas delivery

S270‧‧‧觸媒床氣體回收輸送 S270‧‧‧Catalyst bed gas recovery and transportation

第1圖係為本發明之第一種實施方式的主要步驟流程圖。 Figure 1 is a flowchart of the main steps of the first embodiment of the present invention.

第2圖係為本發明之第一種實施方式的主要架構示意圖。 Figure 2 is a schematic diagram of the main architecture of the first embodiment of the present invention.

第3圖係為本發明之第一種實施方式設有除塵設備的架構示意圖。 FIG. 3 is a schematic diagram of the structure of the first embodiment of the present invention with dust removal equipment.

第4圖係為本發明之第一種實施方式設有濾網裝置的架構示意圖。 FIG. 4 is a schematic diagram of the structure of the first embodiment of the present invention with a filter device.

第5圖係為本發明之第二種實施方式的主要步驟流程圖。 Figure 5 is a flowchart of the main steps of the second embodiment of the present invention.

第6圖係為本發明之第二種實施方式的主要架構示意圖。 FIG. 6 is a schematic diagram of the main structure of the second embodiment of the present invention.

第7圖係為本發明之第二種實施方式設有除塵設備的架構示意圖。 Figure 7 is a schematic diagram of the structure of the second embodiment of the present invention with dust removal equipment.

第8圖係為本發明之第二種實施方式設有濾網裝置的架構示意圖。 Figure 8 is a schematic diagram of the second embodiment of the present invention with a filter device.

請參閱第1~8圖，係為本發明實施例之示意圖，而本發明之觸媒回流高效率有機廢氣處理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，主要是將經過該觸媒床處理之氣體進入該吸附轉輪之吸附區循環利 用，而不經過該煙囪來進行排放，讓該煙囪的排放量降低，並使有機廢氣的處理效率提升。 Please refer to Figures 1 to 8, which are schematic diagrams of embodiments of the present invention. The best implementation of the catalyst reflow high-efficiency organic waste gas treatment system and method of the present invention is applied to the semiconductor industry, optoelectronic industry or chemical-related industries. The volatile organic waste gas treatment system or similar equipment mainly takes the gas processed by the catalyst bed into the adsorption zone of the adsorption rotor for recycling It does not pass through the chimney to discharge, so that the emission of the chimney is reduced, and the treatment efficiency of organic waste gas is improved.

而本發明第一種實施方式的觸媒回流高效率有機廢氣處理系統，主要係設有一觸媒床10、一吸附反應床20、一第一加熱器30、一吸附轉輪40、一第二加熱器50、一第一熱交換器60及一第二熱交換器70(如第2圖至第4圖所示)，其中該第一熱交換器60係設有第一冷側管路601及第一熱側管路602，該第二熱交換器70係設有第二冷側管路701及第二熱側管路702。另該觸媒床10係設有一進氣口11及一出氣口12，而該觸媒床10係主要基本原理是利用觸媒降低其燃燒反應的活化，且進而降低其反應溫度，例如約在250-400℃的環境中處理有機廢氣，以達到節約能源的目的，並於熱機後無需再補充能源，其操作費用較低。 The catalyst reflux high-efficiency organic waste gas treatment system of the first embodiment of the present invention is mainly provided with a catalyst bed 10, an adsorption reaction bed 20, a first heater 30, an adsorption runner 40, and a second The heater 50, a first heat exchanger 60, and a second heat exchanger 70 (as shown in FIGS. 2 to 4), wherein the first heat exchanger 60 is provided with a first cold side pipeline 601 And the first hot side pipeline 602, the second heat exchanger 70 is provided with a second cold side pipeline 701 and a second hot side pipeline 702. In addition, the catalyst bed 10 is provided with an air inlet 11 and an air outlet 12, and the main basic principle of the catalyst bed 10 is to use a catalyst to reduce the activation of the combustion reaction and thereby reduce the reaction temperature, for example, about Organic waste gas is treated in an environment of 250-400°C to achieve the purpose of energy saving, and there is no need to supplement energy after the engine is warmed up, and its operating cost is low.

而該吸附轉輪40係為沸石濃縮轉輪或是其他材質之濃縮轉輪，且該吸附轉輪40內係設有吸附區401、冷卻區402及脫附區402，該吸附轉輪40係設有一廢氣進氣管路41、一淨氣排放管路42、一冷卻氣進氣管路43、一冷卻氣輸送管路44、一熱氣輸送管路45及一脫附濃縮氣體管路46(如第2圖至第4圖所示)，而該廢氣進氣管路41的另一端係連接至該吸附轉輪40之吸附區401的一側，以使該吸附轉輪40之吸附區401吸附該廢氣進氣管路41內的廢氣，且該淨氣排放管路42之一端係與該吸附轉輪40之吸附區401的另一側連接，讓該廢氣經該吸附轉輪40之吸附區401淨化後再由該淨氣排放管路42來輸送，而該淨氣排放管路42的另一端係連接一煙囪，使經由該淨氣 排放管路42所排出淨化後氣體輸送到煙囪90來進行排放。另該淨氣排放管路42係設有一風車421(如第3圖及第4圖所示)，以將該淨氣排放管路42內的氣體推向該煙囪90。 The adsorption runner 40 is a zeolite concentration runner or a concentration runner of other materials, and the adsorption runner 40 is equipped with an adsorption zone 401, a cooling zone 402, and a desorption zone 402. The adsorption runner 40 is It is provided with an exhaust gas inlet pipe 41, a clean gas discharge pipe 42, a cooling gas inlet pipe 43, a cooling gas delivery pipe 44, a hot gas delivery pipe 45 and a desorption concentrated gas pipe 46 ( As shown in Figures 2 to 4), and the other end of the exhaust gas inlet pipe 41 is connected to one side of the adsorption zone 401 of the adsorption runner 40, so that the adsorption zone 401 of the adsorption runner 40 Adsorb the exhaust gas in the exhaust gas inlet pipe 41, and one end of the clean gas discharge pipe 42 is connected to the other side of the adsorption area 401 of the adsorption rotor 40, so that the exhaust gas is adsorbed by the adsorption rotor 40 After the area 401 is purified, it is transported by the clean gas discharge pipeline 42, and the other end of the clean gas discharge pipeline 42 is connected to a chimney, so that the clean gas The purified gas discharged from the discharge pipe 42 is sent to the chimney 90 for discharge. In addition, the clean gas discharge pipeline 42 is provided with a windmill 421 (as shown in FIGS. 3 and 4) to push the gas in the clean gas discharge pipeline 42 toward the chimney 90.

另該冷卻氣進氣管路43的一端係與該吸附轉輪40之冷卻區402的一側連接，而該冷卻氣進氣管路43係有兩種實施態樣，其中第一種實施態樣為該冷卻氣進氣管路43乃是供外氣進入(如第2圖及第3圖所示)，而該外氣係為新鮮空氣，以將該外氣用來輸送到該吸附轉輪40之冷卻區402內提供降溫使用，另第二種實施態樣係該冷卻氣進氣管路43係設有一氣體旁通管路431(如第4圖所示)，該氣體旁通管路431之一端係與該冷卻氣進氣管路43連接，而該氣體旁通管路431之另一端係與該廢氣進氣管路41連接，透過該氣體旁通管路431來將部份的廢氣輸送到該吸附轉輪40之冷卻區402內提供降溫使用。 In addition, one end of the cooling gas intake pipe 43 is connected to one side of the cooling zone 402 of the adsorption runner 40, and the cooling gas intake pipe 43 has two implementation modes, the first one is So the cooling air intake pipe 43 is for external air to enter (as shown in Figures 2 and 3), and the external air system is fresh air to deliver the external air to the adsorption converter The cooling area 402 of the wheel 40 is used for cooling. Another second embodiment is that the cooling gas inlet pipe 43 is provided with a gas bypass pipe 431 (as shown in Fig. 4). The gas bypass pipe One end of the path 431 is connected to the cooling gas inlet pipe 43, and the other end of the gas bypass pipe 431 is connected to the exhaust gas inlet pipe 41. Part of the gas bypass pipe 431 The exhaust gas is transported to the cooling zone 402 of the adsorption rotor 40 for cooling.

另該冷卻氣輸送管路43的一端係與該吸附轉輪40之冷卻區402的另一側連接，而該冷卻氣輸送管路44的另一端係與該第二加熱器50連接，另該第二加熱器50的另一端係與該熱氣輸送管路45的另一端連接(如第2圖至第4圖所示)，其中該第二加熱器50係為電加熱器或是管道加熱器，當為電加熱器時，該電加熱器係採用電熱絲、電熱管或電熱片之其中任一種，而為管道加熱器時，該管道加熱器係採用氣體燃料或液體燃料之其中任一種。而該熱氣輸送管路45的一端係與該吸附轉輪40之脫附區403的另一側連接，且該吸附轉輪40之脫附區403的一側係與該脫附濃縮氣體管路46的一端連接，使將經由該第二加熱器50所提升之熱氣透過該熱氣輸送管路45來傳輸到該吸附轉輪40之脫 附區403來進行脫附使用，並將經過高溫所脫附下來的脫附濃縮氣體透過該脫附濃縮氣體管路46來傳輸運送。另該脫附濃縮氣體管路46係設有一風車461，以將該脫附濃縮氣體管路46內的脫附濃縮氣體進行抽送。 In addition, one end of the cooling gas delivery pipeline 43 is connected to the other side of the cooling zone 402 of the adsorption runner 40, and the other end of the cooling gas delivery pipeline 44 is connected to the second heater 50, and the The other end of the second heater 50 is connected to the other end of the hot gas conveying pipeline 45 (as shown in Figures 2 to 4), wherein the second heater 50 is an electric heater or a pipe heater When it is an electric heater, the electric heater adopts any one of electric heating wire, electric heating tube or electric heating sheet, and when it is a pipeline heater, the pipeline heater adopts either gas fuel or liquid fuel. One end of the hot gas transport pipeline 45 is connected to the other side of the desorption zone 403 of the adsorption runner 40, and one side of the desorption zone 403 of the adsorption runner 40 is connected to the desorption concentrated gas pipeline. One end of 46 is connected so that the hot air lifted by the second heater 50 is transmitted to the adsorption rotor 40 through the hot air delivery pipe 45 The desorption zone 403 is used for desorption, and the desorption concentrated gas desorbed at high temperature is transported through the desorption concentrated gas pipeline 46. In addition, the desorbed concentrated gas pipeline 46 is provided with a windmill 461 to pump the desorbed concentrated gas in the desorbed concentrated gas pipeline 46.

另本發明第一種實施方式中的該冷卻氣輸送管路44與該熱氣輸送管路45之間係設有比例風門，而該比例風門係設有兩種實施設計，其中第一種實施設計乃為該冷卻氣輸送管路44與該熱氣輸送管路45之間設有一連通管路47，且該連通管路47係設有一連通控制閥門471，而該熱氣輸送管路45係設有一熱氣控制閥門451(如第3圖所示)，並透過該連通控制閥門471及該熱氣控制閥門451來形成比例風門，另第二實施設計乃為該冷卻氣輸送管路44與該熱氣輸送管路45之間設有一連通管路47，且該連通管路47係設有一連通控制閥門471，而該冷卻氣輸送管路44係設有一冷卻氣控制閥門441(如第4圖所示)，並透過該連通控制閥門471及該冷卻氣控制閥門441來形成比例風門，藉此，不管是透過該連通控制閥門471及該熱氣控制閥門451之設計的比例風門或是透過該連通控制閥門471及該冷卻氣控制閥門441之設計的比例風門，皆能調整控制風力之大小，讓該熱氣輸送管路45內的溫度保持一定高溫來提供給該吸附轉輪40之脫附區403使用。 In addition, in the first embodiment of the present invention, a proportional damper is provided between the cooling gas conveying pipe 44 and the hot gas conveying pipe 45, and the proportional damper is provided with two implementation designs, of which the first implementation design A communicating pipe 47 is provided between the cooling gas conveying pipe 44 and the hot gas conveying pipe 45, and the communicating pipe 47 is provided with a communicating control valve 471, and the hot gas conveying pipe 45 is provided with There is a hot gas control valve 451 (as shown in Figure 3), and a proportional damper is formed through the communication control valve 471 and the hot gas control valve 451. Another second implementation design is for the cooling gas delivery pipeline 44 and the hot gas delivery A connecting pipeline 47 is provided between the pipelines 45, and the connecting pipeline 47 is provided with a connecting control valve 471, and the cooling gas delivery pipeline 44 is provided with a cooling gas control valve 441 (as shown in Figure 4). Show), and through the communication control valve 471 and the cooling gas control valve 441 to form a proportional damper, thereby, whether through the communication control valve 471 and the hot gas control valve 451 design proportional damper or through the communication control Both the valve 471 and the proportional damper designed for the cooling gas control valve 441 can adjust and control the size of the wind force, so that the temperature in the hot gas conveying pipe 45 can be maintained at a certain high temperature to be used by the desorption zone 403 of the adsorption rotor 40 .

再者，該第一熱交換器60係連接有一第一熱氣回收管路61、一第一觸媒床熱氣回收管路62及一第一脫附濃縮氣體輸送管路63(如第2圖至第4圖所示)，該第一觸媒床熱氣回收管路62的一端係與該第一熱交換器60之第一熱側管路602的一端連接，該第一觸媒床熱氣回 收管路62的另一端係與該觸媒床10之出氣口12連接，該第一熱氣回收管路61的一端係與該第一熱交換器60之第一熱側管路602的另一端連接，該第一脫附濃縮氣體輸送管路63的一端係與該第一熱交換器60之第一冷側管路601的另一端連接。 Furthermore, the first heat exchanger 60 is connected to a first hot gas recovery pipeline 61, a first catalyst bed hot gas recovery pipeline 62, and a first desorption concentrated gas delivery pipeline 63 (as shown in Figures 2 to As shown in Figure 4), one end of the first catalyst bed hot gas recovery pipeline 62 is connected to one end of the first hot side pipeline 602 of the first heat exchanger 60, and the first catalyst bed hot gas return The other end of the collecting pipe 62 is connected to the gas outlet 12 of the catalyst bed 10, and one end of the first hot gas recovery pipe 61 is connected to the other end of the first hot side pipe 602 of the first heat exchanger 60 Connected, one end of the first desorption concentrated gas delivery pipeline 63 is connected to the other end of the first cold side pipeline 601 of the first heat exchanger 60.

另該第一脫附濃縮氣體輸送管路63的另一端係與該第一加熱器30之一端連接(如第2圖至第4圖所示)，其中該第一加熱器30係為電加熱器或是管道加熱器，當為電加熱器時，該電加熱器係採用電熱絲、電熱管或電熱片之其中任一種，而為管道加熱器時，該管道加熱器係採用氣體燃料或液體燃料之其中任一種。且該第一加熱器30係設有一第一加熱器輸送管路31(如第2圖至第4圖所示)，該第一加熱器輸送管路31之另一端係與該吸附反應床20之一端連接，其中該吸附反應床20係設有一吸附反應床輸送管路21(如第2圖至第4圖所示)，該吸附反應床輸送管路21之另一端係與該觸媒床10之進氣口11連接，而該吸附反應床20係為具多孔之材質，以用來將含矽的有機化合物進行反應成為二氧化矽(SiO2)等微粒並吸附。 In addition, the other end of the first desorption concentrated gas delivery pipeline 63 is connected to one end of the first heater 30 (as shown in Figures 2 to 4), wherein the first heater 30 is electrically heated When it is an electric heater, the electric heater adopts any one of electric heating wire, electric heating tube or electric heating piece, and when it is a pipeline heater, the pipeline heater adopts gas fuel or liquid Any of the fuels. And the first heater 30 is provided with a first heater delivery pipe 31 (as shown in Figures 2 to 4), and the other end of the first heater delivery pipe 31 is connected to the adsorption reaction bed 20 One end is connected, wherein the adsorption reaction bed 20 is provided with an adsorption reaction bed transport pipeline 21 (as shown in Figures 2 to 4), and the other end of the adsorption reaction bed transport pipeline 21 is connected to the catalyst bed The air inlet 11 of 10 is connected, and the adsorption reaction bed 20 is made of porous material for reacting organic compounds containing silicon into particles such as silicon dioxide (SiO 2 ) and adsorbing them.

另該第二熱交換器70係連接有一第二脫附濃縮氣體輸送管路71及一第二熱氣回收管路72(如第2圖至第4圖所示)，該第二熱交換器70之第二冷側管路701的一端係與該脫附濃縮氣體管路46的另一端連接，該第二脫附濃縮氣體輸送管路71的一端係與該第二熱交換器70之第二冷側管路701的另一端連接，該第二脫附濃縮氣體輸送管路71的另一端係與該第一熱交換器60之第一冷側管路301的一端連接，該第二熱氣回收管路72的一端係與該第二熱交換器70之第二熱側 管路702的一端連接，該第二熱氣回收管路72的另一端係與該廢氣進氣管路41連接，該第二熱交換器70之第二熱側管路702的另一端係與該第一熱氣回收管路61的另一端連接。 In addition, the second heat exchanger 70 is connected to a second desorption concentrated gas delivery pipeline 71 and a second hot gas recovery pipeline 72 (as shown in FIGS. 2 to 4). The second heat exchanger 70 One end of the second cold-side pipeline 701 is connected to the other end of the desorption concentrated gas pipeline 46, and one end of the second desorption concentrated gas delivery pipeline 71 is connected to the second end of the second heat exchanger 70 The other end of the cold side pipeline 701 is connected, and the other end of the second desorption concentrated gas delivery pipeline 71 is connected to one end of the first cold side pipeline 301 of the first heat exchanger 60, and the second hot gas is recovered One end of the pipe 72 is connected to the second hot side of the second heat exchanger 70 One end of the pipe 702 is connected, the other end of the second hot gas recovery pipe 72 is connected to the exhaust gas inlet pipe 41, and the other end of the second hot side pipe 702 of the second heat exchanger 70 is connected to the The other end of the first hot gas recovery pipe 61 is connected.

而本發明係於該第二熱交換器70之第二熱氣回收管路72上係設有一除塵設備721(如第3圖所示)，該除塵設備721係為袋式除塵器、電袋式複合除塵器、慣性除塵器、靜電除塵器、離心式除塵器、濾筒式脈衝除塵器、脈衝袋式除塵器、脈衝濾芯除塵器、脈衝噴吹袋式除塵器、濕式除塵器、濕式電除塵器、濕式靜電除塵器、水膜除塵器、文丘里管除塵器、旋風分離器、煙道除塵器、多層除塵器、負壓反吹濾袋除塵器、低壓長袋脈衝除塵器、臥式靜電除塵器、無動力除塵器、荷電水霧除塵器、多管旋風除塵器、防爆除塵器之其中任一，或是於該第二熱交換器70之第二熱氣回收管路72設有一濾網裝置722(如第4圖所示)，透過該除塵設備721或是該濾網裝置722來將要進入該廢氣進氣管路41的熱氣先進行除塵或過濾。 In the present invention, a dust removal device 721 (as shown in Figure 3) is provided on the second hot gas recovery pipe 72 of the second heat exchanger 70. The dust removal device 721 is a bag filter, an electric bag type Composite dust collector, inertial dust collector, electrostatic dust collector, centrifugal dust collector, cartridge pulse dust collector, pulse bag filter, pulse filter dust collector, pulse jet bag filter, wet dust collector, wet type Electrostatic precipitator, wet electrostatic precipitator, water film dust collector, venturi tube dust collector, cyclone separator, flue dust collector, multi-layer dust collector, negative pressure back blow filter bag dust collector, low pressure long bag pulse dust collector, Any one of horizontal electrostatic precipitator, unpowered precipitator, charged water mist precipitator, multi-tube cyclone precipitator, explosion-proof precipitator, or installed in the second hot gas recovery pipeline 72 of the second heat exchanger 70 There is a filter device 722 (as shown in FIG. 4), through the dust removal equipment 721 or the filter device 722, the hot air entering the exhaust gas inlet pipe 41 is first dusted or filtered.

藉此，讓該吸附轉輪40之脫附區403所脫附下來的脫附濃縮氣體透過該脫附濃縮氣體管路46來傳輸到該第二熱交換器70之第二冷側管路701來進行熱交換，並再透過該第二脫附濃縮氣體輸送管路71來傳輸到該第一熱交換器60之第一冷側管路601來進行熱交換後，再以第一脫附濃縮氣體輸送管路63來輸送到該第一加熱器30，透過該第一加熱器30來將所輸送過來脫附濃縮氣體進行加熱以提高脫附濃縮氣體之溫度，再將提高溫度之脫附濃縮氣體透過該第一加熱器輸送管路31來輸送至該吸附反應床20，使該吸附反應床20將含矽的化合物反 應成為二氧化矽(SiO2)並吸附，再由該吸附反應床輸送管路21來輸送到觸媒床10內進行處理。 Thereby, the desorbed concentrated gas desorbed from the desorption zone 403 of the adsorption rotor 40 is transmitted to the second cold side pipe 701 of the second heat exchanger 70 through the desorbed concentrated gas pipe 46 To perform heat exchange, and then to the first cold-side pipe 601 of the first heat exchanger 60 through the second desorption concentrated gas delivery pipe 71 for heat exchange, and then the first desorption concentration The gas delivery pipe 63 is used to deliver to the first heater 30, and the delivered desorption concentrated gas is heated through the first heater 30 to increase the temperature of the desorption concentrated gas, and then the desorption concentrated gas with the increased temperature The gas is transported to the adsorption reaction bed 20 through the first heater delivery pipe 31, so that the adsorption reaction bed 20 reacts silicon-containing compounds into silicon dioxide (SiO 2 ) and adsorbs it, and then is transported by the adsorption reaction bed The pipeline 21 is transported to the catalyst bed 10 for processing.

當該觸媒床10進行處理後，即透過與該觸媒床10之出氣口12所連接的第一觸媒床熱氣回收管路62來將該觸媒床10處理之熱氣回收到該第一熱交換器60之第一熱側管路602內進行熱交換，再透過該第一熱氣回收管路61來輸送到該第二熱交換器70之第二熱側管路702內進行熱交換，且再經由該第二熱氣回收管路72來輸送到該廢氣進氣管路41內，使經過該觸媒床10處理之氣體進入該吸附轉輪40之吸附區401循環利用，而不經過該煙囪90來進行排放，讓該煙囪90的排放量降低，並使有機廢氣的處理效率提升。 After the catalyst bed 10 is processed, the hot gas from the catalyst bed 10 is recovered to the first catalyst bed through the first catalyst bed hot gas recovery pipeline 62 connected to the outlet 12 of the catalyst bed 10 The heat exchange is carried out in the first hot-side pipe 602 of the heat exchanger 60, and then sent to the second hot-side pipe 702 of the second heat exchanger 70 through the first hot gas recovery pipe 61 for heat exchange. And then through the second hot gas recovery pipeline 72 to transport into the exhaust gas inlet pipeline 41, so that the gas processed by the catalyst bed 10 enters the adsorption zone 401 of the adsorption rotor 40 for recycling, without passing through the The chimney 90 is used to discharge, so that the emission of the chimney 90 is reduced, and the treatment efficiency of the organic waste gas is improved.

而本發明第一種實施方式的觸媒回流高效率有機廢氣處理方法，其主要係用於有機廢氣處理系統，且包括有一觸媒床10、一吸附反應床20、一第一加熱器30、一吸附轉輪40、一第二加熱器50、一第一熱交換器60及一第二熱交換器70(如第2圖至第4圖所示)，該吸附轉輪40係設有吸附區401、冷卻區402及脫附區403，該吸附轉輪40係連接有一廢氣進氣管路41、一淨氣排放管路42、一冷卻氣進氣管路43、一冷卻氣輸送管路44、一熱氣輸送管路45及一脫附濃縮氣體管路46，該第一熱交換器60係設有第一冷側管路601及第一熱側管路602，該第一熱交換器60係連接有一第一熱氣回收管路61、一第一觸媒床熱氣回收管路62及一第一脫附濃縮氣體輸送管路63，該第二熱交換器70係設有第二冷側管路701及第二熱側管路702，該第二熱交換器70係連接有一第二脫附濃縮氣體輸送管路71及一 第二熱氣回收管路72，該第一加熱器30係設有一第一加熱器輸送管路31，該吸附反應床20係設有一吸附反應床輸送管路21。 The catalyst reflux high-efficiency organic waste gas treatment method of the first embodiment of the present invention is mainly used in an organic waste gas treatment system, and includes a catalyst bed 10, an adsorption reaction bed 20, a first heater 30, An adsorption runner 40, a second heater 50, a first heat exchanger 60 and a second heat exchanger 70 (as shown in Figures 2 to 4), the adsorption runner 40 is equipped with adsorption Zone 401, cooling zone 402 and desorption zone 403, the adsorption runner 40 is connected with an exhaust gas inlet pipe 41, a clean gas discharge pipe 42, a cooling gas inlet pipe 43, and a cooling gas delivery pipe 44. A hot gas delivery pipeline 45 and a desorption concentrated gas pipeline 46. The first heat exchanger 60 is provided with a first cold side pipeline 601 and a first hot side pipeline 602, the first heat exchanger 60 is connected to a first hot gas recovery pipeline 61, a first catalyst bed hot gas recovery pipeline 62, and a first desorption concentrated gas delivery pipeline 63. The second heat exchanger 70 is provided with a second cold side Pipeline 701 and second hot-side pipeline 702, the second heat exchanger 70 is connected with a second desorption concentrated gas delivery pipeline 71 and a The second hot gas recovery pipeline 72 is provided with a first heater delivery pipeline 31 for the first heater 30, and an adsorption reaction bed delivery pipeline 21 for the adsorption reaction bed 20.

而該處理方法的主要步驟(如第1圖所示)係包括：步驟S100吸附區吸附：將廢氣透過該廢氣進氣管路41的另一端來送入該吸附轉輪40之吸附區401的一側進行吸附，再將吸附後之氣體透過該淨氣排放管路42的另一端來進行輸送。而完成上述步驟S100後即進行下一步驟S110。 The main steps of the treatment method (as shown in Figure 1) include: step S100 adsorption zone adsorption: the exhaust gas is sent to the adsorption zone 401 of the adsorption rotor 40 through the other end of the exhaust gas inlet pipe 41 One side is adsorbed, and the adsorbed gas is transmitted through the other end of the clean gas discharge pipeline 42. After the above step S100 is completed, the next step S110 is performed.

其中上述之步驟S100中該淨氣排放管路42的另一端係連接一煙囪90(如第2圖至第4圖所示)，讓經由該淨氣排放管路42所排出淨化後氣體輸送到煙囪90來進行排放。另該淨氣排放管路42係設有一風車421(如第3圖及第4圖所示)，以將該淨氣排放管路42內的氣體推向該煙囪90。 The other end of the clean gas discharge pipeline 42 in the above step S100 is connected to a chimney 90 (as shown in Figures 2 to 4), so that the purified gas discharged through the clean gas discharge pipeline 42 is transported to The chimney 90 is used for discharge. In addition, the clean gas discharge pipeline 42 is provided with a windmill 421 (as shown in FIGS. 3 and 4) to push the gas in the clean gas discharge pipeline 42 toward the chimney 90.

另，下一步進行的步驟S110冷卻區冷卻：透過該冷卻氣進氣管路43的另一端來輸送冷卻氣至該吸附轉輪40之冷卻區402進行冷卻，再透過該冷卻氣輸送管路44的另一端來將經過冷卻區402之冷卻氣輸送到該第二加熱器50內。而完成上述步驟S110後即進行下一步驟S120。 In addition, the next step S110 cooling zone cooling: the cooling air is delivered to the cooling zone 402 of the adsorption runner 40 through the other end of the cooling air inlet pipe 43 for cooling, and then through the cooling air delivery pipe 44 The other end of the cooling zone 402 is used to deliver the cooling air to the second heater 50. After the above step S110 is completed, the next step S120 is performed.

其中該上述之步驟S110中該第二加熱器50係為電加熱器或是管道加熱器，當為電加熱器時，該電加熱器係採用電熱絲、電熱管或電熱片之其中任一種，而為管道加熱器時，該管道加熱器係採用氣體燃料或液體燃料之其中任一種。另該冷卻氣進氣管路43的一端係與該吸附轉輪40之冷卻區402的一側連接，而該冷卻氣進氣管路43係有兩 種實施態樣，其中第一種實施態樣為該冷卻氣進氣管路43乃是供外氣進入(如第2圖及第3圖所示)，而該外氣係為新鮮空氣，以將該外氣用來輸送到該吸附轉輪40之冷卻區402內提供降溫使用，另第二種實施態樣係該冷卻氣進氣管路43係設有一氣體旁通管路431(如第4圖所示)，該氣體旁通管路431之一端係與該冷卻氣進氣管路43連接，而該氣體旁通管路431之另一端係與該廢氣進氣管路41連接，透過該氣體旁通管路431來將部份的廢氣輸送到該吸附轉輪40之冷卻區402內提供降溫使用。 Wherein the second heater 50 in the above step S110 is an electric heater or a pipe heater. When it is an electric heater, the electric heater uses any one of electric heating wire, electric heating tube or electric heating fin, In the case of a pipeline heater, the pipeline heater uses either gas fuel or liquid fuel. In addition, one end of the cooling air inlet pipe 43 is connected to one side of the cooling zone 402 of the adsorption rotor 40, and the cooling air inlet pipe 43 has two In the first embodiment, the cooling air intake pipe 43 is for external air to enter (as shown in Figures 2 and 3), and the external air system is fresh air. The external air is transported to the cooling zone 402 of the adsorption runner 40 for cooling. Another second embodiment is that the cooling air inlet pipe 43 is provided with a gas bypass pipe 431 (such as 4), one end of the gas bypass pipe 431 is connected to the cooling gas inlet pipe 43, and the other end of the gas bypass pipe 431 is connected to the exhaust gas inlet pipe 41 through The gas bypass pipeline 431 transports part of the exhaust gas to the cooling zone 402 of the adsorption rotor 40 for cooling.

另，下一步進行的步驟S120脫附區脫附：透過與該第二加熱器50的另一端所連接的熱氣輸送管路44來將熱氣體輸送到該吸附轉輪40之脫附區403進行脫附，再透過該脫附濃縮氣體管路46的另一端來將脫附濃縮氣體輸送到第二熱交換器70之第二冷側管路701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 desorption zone desorption: the hot gas is transported to the desorption zone 403 of the adsorption rotor 40 through the hot gas delivery pipe 44 connected to the other end of the second heater 50. After desorption, the desorption concentrated gas is transported to one end of the second cold side pipe 701 of the second heat exchanger 70 through the other end of the desorption concentrated gas pipeline 46. After the above step S120 is completed, the next step S130 is performed.

其中該上述之步驟S120中該脫附濃縮氣體管路46係設有一風車461，以將該脫附濃縮氣體管路46內的脫附濃縮氣體進行抽送。另該冷卻氣輸送管路44與該熱氣輸送管路45之間係設有比例風門，而該比例風門係設有兩種實施設計，其中第一種實施設計乃為該冷卻氣輸送管路44與該熱氣輸送管路45之間設有一連通管路47，且該連通管路47係設有一連通控制閥門471，而該熱氣輸送管路45係設有一熱氣控制閥門451(如第3圖所示)，並透過該連通控制閥門471及該熱氣控制閥門451來形成比例風門。另第二實施設計乃為該冷卻氣輸送管路44與該熱氣輸送管路45之間設有一連通管路47，且該連通管路 47係設有一連通控制閥門471，而該冷卻氣輸送管路44係設有一冷卻氣控制閥門441(如第4圖所示)，並透過該連通控制閥門471及該冷卻氣控制閥門441來形成比例風門。藉此，不管是透過該連通控制閥門471及該熱氣控制閥門451之設計的比例風門或是透過該連通控制閥門471及該冷卻氣控制閥門441之設計的比例風門，皆能調整控制風力之大小，讓該熱氣輸送管路45內的溫度保持一定高溫來提供給該吸附轉輪40之脫附區403使用。 In the step S120 described above, the desorbed concentrated gas pipeline 46 is provided with a windmill 461 to pump the desorbed concentrated gas in the desorbed concentrated gas pipeline 46. In addition, a proportional damper is provided between the cooling gas conveying pipeline 44 and the hot gas conveying pipeline 45, and the proportional damper is provided with two implementation designs. The first implementation design is the cooling gas delivery pipeline 44 A connecting pipe 47 is provided with the hot gas conveying pipe 45, and the connecting pipe 47 is provided with a connecting control valve 471, and the hot gas conveying pipe 45 is provided with a hot gas control valve 451 (such as the third As shown in the figure), a proportional damper is formed through the communication control valve 471 and the hot gas control valve 451. Another second implementation design is that a communicating pipe 47 is provided between the cooling gas conveying pipe 44 and the hot gas conveying pipe 45, and the communicating pipe 47 is provided with a communication control valve 471, and the cooling gas delivery pipeline 44 is provided with a cooling gas control valve 441 (as shown in Figure 4), and through the communication control valve 471 and the cooling gas control valve 441 Form a proportional throttle. Thereby, regardless of the proportional damper designed through the communication control valve 471 and the hot gas control valve 451 or the proportional damper designed through the communication control valve 471 and the cooling gas control valve 441, the magnitude of the control wind can be adjusted. , Keep the temperature in the hot gas conveying pipeline 45 at a certain high temperature to provide the desorption zone 403 of the adsorption rotor 40 for use.

另，下一步進行的步驟S130脫附濃縮氣體輸送：該脫附濃縮氣體再透過該第二熱交換器70之第二冷側管路701的另一端所連接的第二脫附濃縮氣體輸送管路71來輸送到該第一熱交換器60之第一冷側管路601的一端，並再透過該第一熱交換器60之第一冷側管路601的另一端所連接的第一脫附濃縮氣體輸送管路63來輸送到該第一加熱器30內。而完成上述步驟S130後即進行下一步驟S140。 In addition, the next step S130 desorption concentrated gas delivery: the desorption concentrated gas then passes through the second desorption concentrated gas delivery pipe connected to the other end of the second cold side pipeline 701 of the second heat exchanger 70 The path 71 is transported to one end of the first cold-side pipe 601 of the first heat exchanger 60, and then passes through the first cold-side pipe 601 connected to the other end of the first heat exchanger 60. The concentrated gas delivery pipe 63 is attached to deliver it to the first heater 30. After the above step S130 is completed, the next step S140 is performed.

其中該上述之步驟S130中該第一加熱器30係為電加熱器或是管道加熱器，當為電加熱器時，該電加熱器係採用電熱絲、電熱管或電熱片之其中任一種，而為管道加熱器時，該管道加熱器係採用氣體燃料或液體燃料之其中任一種。 Wherein the first heater 30 in the above step S130 is an electric heater or a pipe heater. When it is an electric heater, the electric heater uses any one of an electric heating wire, an electric heating tube or an electric heating sheet, In the case of a pipeline heater, the pipeline heater uses either gas fuel or liquid fuel.

另，下一步進行的步驟S140吸附反應床吸附：將經由該第一加熱器30進行加熱升溫的脫附濃縮氣體透過該第一加熱器輸送管路31來輸送至該吸附反應床20來進行吸附，其中該吸附反應床20係為具多孔之材質，以用來將含矽的有機化合物進行反應成為二氧化矽(SiO2)等微粒並吸附。而完成上述步驟S140後即進行下一步驟S150。 In addition, the next step S140 is the adsorption reaction bed adsorption: the desorption concentrated gas heated by the first heater 30 is sent to the adsorption reaction bed 20 through the first heater delivery pipe 31 for adsorption. Wherein, the adsorption reaction bed 20 is made of a porous material for reacting organic compounds containing silicon into particles such as silicon dioxide (SiO 2 ) and adsorbing them. After the above step S140 is completed, the next step S150 is performed.

另，下一步進行的步驟S150觸媒床處理：將經過該吸附反應床20進行吸附的脫附濃縮氣體再透過該吸附反應床輸送管路21來輸送到觸媒床10內進行處理。而完成上述步驟S150後即進行下一步驟S160。 In addition, the next step S150 catalyst bed treatment: the desorption concentrated gas that has been adsorbed by the adsorption reaction bed 20 is transported to the catalyst bed 10 through the adsorption reaction bed delivery pipeline 21 for processing. After the above step S150 is completed, the next step S160 is performed.

另，下一步進行的步驟S160觸媒床氣體輸送：將經過觸媒床10處理後之氣體透過該觸媒床10之出氣口12所連接的第一觸媒床熱氣回收管路62輸送到該第一熱交換器60之第一熱側管路602的一端，再由該第一熱交換器60之第一熱側管路602的另一端所連接的第一熱氣回收管路61輸送到該第二熱交換器70之第二熱側管路702的一端。而完成上述步驟S160後即進行下一步驟S170。 In addition, the next step S160 catalyst bed gas transportation: the gas after the catalyst bed 10 is transported to the first catalyst bed hot gas recovery pipeline 62 connected to the gas outlet 12 of the catalyst bed 10 One end of the first hot-side pipe 602 of the first heat exchanger 60 is transported to the first hot gas recovery pipe 61 connected to the other end of the first hot-side pipe 602 of the first heat exchanger 60 One end of the second hot side pipe 702 of the second heat exchanger 70. After the above step S160 is completed, the next step S170 is performed.

另，下一步進行的步驟S170觸媒床氣體回收輸送：將輸送到該第二熱交換器70之第二熱側管路702的觸媒床10之氣體，再經由與該第二熱交換器70之第二熱側管路702的另一端所連接的第二熱氣回收管路72來輸送到該廢氣進氣管路41連接。 In addition, the next step S170 is the catalyst bed gas recovery and transportation: the gas sent to the catalyst bed 10 of the second hot side pipeline 702 of the second heat exchanger 70 is passed through the second heat exchanger The second hot gas recovery pipe 72 connected to the other end of the second hot side pipe 702 of 70 is connected to the exhaust gas intake pipe 41.

其中該上述之步驟S170中該第二熱交換器70之第二熱氣回收管路72係設有一除塵設備721(如第3圖所示)，該除塵設備721係為袋式除塵器、電袋式複合除塵器、慣性除塵器、靜電除塵器、離心式除塵器、濾筒式脈衝除塵器、脈衝袋式除塵器、脈衝濾芯除塵器、脈衝噴吹袋式除塵器、濕式除塵器、濕式電除塵器、濕式靜電除塵器、水膜除塵器、文丘里管除塵器、旋風分離器、煙道除塵器、多層除塵器、負壓反吹濾袋除塵器、低壓長袋脈衝除塵器、臥式靜電除塵器、無動力除塵器、荷電水霧除塵器、多管旋風除塵器、防爆除塵器之其中任一，或是於該第 二熱交換器70之第二熱氣回收管路72設有一濾網裝置722(如第4圖所示)，透過該除塵設備721或是該濾網裝置722來將要進入該廢氣進氣管路41的熱氣先進行除塵或過濾。 In the above step S170, the second hot gas recovery pipe 72 of the second heat exchanger 70 is provided with a dust removal device 721 (as shown in Figure 3), and the dust removal device 721 is a bag filter, an electric bag Type composite dust collector, inertial dust collector, electrostatic dust collector, centrifugal dust collector, filter cartridge pulse dust collector, pulse bag filter, pulse filter dust collector, pulse jet bag dust collector, wet dust collector, wet Type electrostatic precipitator, wet electrostatic precipitator, water film dust collector, venturi tube dust collector, cyclone separator, flue dust collector, multi-layer dust collector, negative pressure back blow filter bag dust collector, low pressure long bag pulse dust collector , Horizontal electrostatic precipitator, unpowered precipitator, charged water mist precipitator, multi-tube cyclone precipitator, explosion-proof precipitator, or any one of the The second hot gas recovery pipeline 72 of the second heat exchanger 70 is provided with a filter device 722 (as shown in Fig. 4), through which the dust removal equipment 721 or the filter device 722 will enter the exhaust gas intake pipeline 41 The hot air is first dusted or filtered.

藉此，讓該吸附轉輪40之脫附區403所脫附下來的脫附濃縮氣體透過該脫附濃縮氣體管路46來傳輸到該第二熱交換器70之第二冷側管路701來進行熱交換，並再透過該第二脫附濃縮氣體輸送管路71來傳輸到該第一熱交換器60之第一冷側管路601來進行熱交換後，再以第一脫附濃縮氣體輸送管路63來輸送到該第一加熱器30，透過該第一加熱器30來將所輸送過來脫附濃縮氣體進行加熱以提高脫附濃縮氣體之溫度，再將提高溫度之脫附濃縮氣體透過該第一加熱器輸送管路31來輸送至該吸附反應床20，使該吸附反應床20將含有矽的有機化合物反應成二氧化矽(SiO2)並吸附，再由該吸附反應床輸送管路21來輸送到觸媒床10內進行處理。 Thereby, the desorbed concentrated gas desorbed from the desorption zone 403 of the adsorption rotor 40 is transmitted to the second cold side pipe 701 of the second heat exchanger 70 through the desorbed concentrated gas pipe 46 To perform heat exchange, and then to the first cold side pipe 601 of the first heat exchanger 60 through the second desorption concentrated gas delivery pipe 71 for heat exchange, and then the first desorption concentration The gas delivery pipe 63 is used to deliver to the first heater 30, and the delivered desorption concentrated gas is heated through the first heater 30 to increase the temperature of the desorption concentrated gas, and then the desorption concentrated gas with the increased temperature The gas is transported to the adsorption reaction bed 20 through the first heater delivery pipe 31, so that the adsorption reaction bed 20 reacts organic compounds containing silicon into silicon dioxide (SiO 2 ) and adsorbs it, and then the adsorption reaction bed The conveying pipe 21 is conveyed into the catalyst bed 10 for processing.

當該觸媒床10進行處理後，即透過與該觸媒床10之出氣口12所連接的第一觸媒床熱氣回收管路62來將該觸媒床10處理之熱氣回收到該第一熱交換器60之第一熱側管路602內進行熱交換，再透過該第一熱氣回收管路61來輸送到該第二熱交換器70之第二熱側管路702內進行熱交換，且再經由該第二熱氣回收管路72來輸送到該廢氣進氣管路41內，使經過該觸媒床10處理之氣體進入該吸附轉輪40之吸附區401循環利用，而不經過該煙囪90來進行排放，讓該煙囪90的排放量降低，並使有機廢氣的處理效率提升。 After the catalyst bed 10 is processed, the hot gas from the catalyst bed 10 is recovered to the first catalyst bed through the first catalyst bed hot gas recovery pipeline 62 connected to the outlet 12 of the catalyst bed 10 The heat exchange is carried out in the first hot-side pipe 602 of the heat exchanger 60, and then sent to the second hot-side pipe 702 of the second heat exchanger 70 through the first hot gas recovery pipe 61 for heat exchange. And then through the second hot gas recovery pipeline 72 to transport into the exhaust gas inlet pipeline 41, so that the gas processed by the catalyst bed 10 enters the adsorption zone 401 of the adsorption rotor 40 for recycling, without passing through the The chimney 90 is used to discharge, so that the emission of the chimney 90 is reduced, and the treatment efficiency of the organic waste gas is improved.

另，本發明第二種實施方式的觸媒回流高效率有機廢氣處理 系統，主要係設有一觸媒床10、一吸附反應床20、一第一加熱器30、一吸附轉輪40、一第二加熱器50、一第二熱交換器70及一冷卻器80(如第6圖至第8圖所示)，其中該第二熱交換器70係設有第二冷側管路701及第二熱側管路702，而該冷卻器80係設有冷卻水管路801。另該觸媒床10係設有一進氣口11及一出氣口12，而該觸媒床10係主要基本原理是利用觸媒降低其燃燒反應的活化，且進而降低其反應溫度，例如約在250-400℃的環境中處理有機廢氣，以達到節約能源的目的，並於熱機後無需再補充能源，其操作費用較低。 In addition, the second embodiment of the present invention is a catalyst reflux high-efficiency organic waste gas treatment The system mainly includes a catalyst bed 10, an adsorption reaction bed 20, a first heater 30, an adsorption rotor 40, a second heater 50, a second heat exchanger 70 and a cooler 80 ( As shown in Figures 6 to 8), the second heat exchanger 70 is provided with a second cold side pipe 701 and a second hot side pipe 702, and the cooler 80 is provided with a cooling water pipe 801. In addition, the catalyst bed 10 is provided with an air inlet 11 and an air outlet 12, and the main basic principle of the catalyst bed 10 is to use a catalyst to reduce the activation of the combustion reaction and thereby reduce the reaction temperature, for example, about Organic waste gas is treated in an environment of 250-400°C to achieve the purpose of energy saving, and there is no need to supplement energy after the engine is warmed up, and its operating cost is low.

而該吸附轉輪40係為沸石濃縮轉輪或是其他材質之濃縮轉輪，且該吸附轉輪40內係設有吸附區401、冷卻區402及脫附區403，該吸附轉輪40係設有一廢氣進氣管路41、一淨氣排放管路42、一冷卻氣進氣管路43、一冷卻氣輸送管路44、一熱氣輸送管路45及一脫附濃縮氣體管路46(如第6圖至第8圖所示)，而該廢氣進氣管路41的另一端係連接至該吸附轉輪40之吸附區401的一側，以使該吸附轉輪之吸附區吸附該廢氣進氣管路41內的廢氣，且該淨氣排放管路42之一端係與該吸附轉輪40之吸附區401的另一側連接，讓該廢氣經該吸附轉輪40之吸附區401淨化後再由該淨氣排放管路42來輸送，而該淨氣排放管路42的另一端係連接一煙囪90(如第6圖至第8圖所示)，使經由該淨氣排放管路42所排出淨化後氣體輸送到煙囪90來進行排放。另該淨氣排放管路42係設有一風車421(如第7圖及第8圖所示)，以將該淨氣排放管路42內的氣體推向該煙囪90。 The adsorption runner 40 is a zeolite concentration runner or a concentration runner of other materials, and the adsorption runner 40 is provided with an adsorption zone 401, a cooling zone 402, and a desorption zone 403. The adsorption runner 40 is It is provided with an exhaust gas inlet pipe 41, a clean gas discharge pipe 42, a cooling gas inlet pipe 43, a cooling gas delivery pipe 44, a hot gas delivery pipe 45 and a desorption concentrated gas pipe 46 ( As shown in Figures 6 to 8), the other end of the exhaust gas inlet pipe 41 is connected to one side of the adsorption zone 401 of the adsorption runner 40, so that the adsorption zone of the adsorption runner can adsorb the The exhaust gas in the exhaust gas inlet pipe 41, and one end of the clean gas discharge pipe 42 is connected to the other side of the adsorption area 401 of the adsorption rotor 40, so that the exhaust gas passes through the adsorption area 401 of the adsorption rotor 40 After purification, it is transported by the clean gas discharge pipe 42, and the other end of the clean gas discharge pipe 42 is connected to a chimney 90 (as shown in Figs. 6 to 8), so that the clean gas discharge pipe The purified gas discharged from the path 42 is sent to the chimney 90 for discharge. In addition, the clean gas discharge pipeline 42 is provided with a windmill 421 (as shown in FIGS. 7 and 8) to push the gas in the clean gas discharge pipeline 42 toward the chimney 90.

另該冷卻氣進氣管路43的一端係與該吸附轉輪40之冷 卻區402的一側連接，而該冷卻氣進氣管路43係有兩種實施態樣，其中第一種實施態樣為該冷卻氣進氣管路43乃是供外氣進入(如第6圖及第7圖所示)，而該外氣係為新鮮空氣，以將該外氣用來輸送到該吸附轉輪40之冷卻區402內提供降溫使用，另第二種實施態樣係該冷卻氣進氣管路43係設有一氣體旁通管路431(如第8圖所示)，該氣體旁通管路431之一端係與該冷卻氣進氣管路43連接，而該氣體旁通管路431之另一端係與該廢氣進氣管路41連接，透過該氣體旁通管路431來將部份的廢氣輸送到該吸附轉輪40之冷卻區402內提供降溫使用。 In addition, one end of the cooling air inlet pipe 43 is connected to the cooling of the adsorption runner 40 One side of the cooling zone 402 is connected, and the cooling air intake pipe 43 has two implementation modes. The first implementation mode is that the cooling air intake pipe 43 is for external air to enter (such as 6 and 7), and the external air system is fresh air, so that the external air is used to transport the external air to the cooling zone 402 of the adsorption rotor 40 for cooling use. Another second implementation mode is The cooling gas inlet pipe 43 is provided with a gas bypass pipe 431 (as shown in Fig. 8). One end of the gas bypass pipe 431 is connected to the cooling gas inlet pipe 43, and the gas The other end of the bypass pipeline 431 is connected to the exhaust gas inlet pipeline 41, and part of the exhaust gas is delivered to the cooling zone 402 of the adsorption rotor 40 through the gas bypass pipeline 431 for cooling.

另該冷卻氣輸送管路44的一端係與該吸附轉輪40之冷卻區402的另一側連接，而該冷卻氣輸送管路44的另一端係與該第二加熱器50連接，另該第二加熱器50的另一端係與該熱氣輸送管路45的另一端連接(如第6圖至第8圖所示)，其中該第二加熱器50係為電加熱器或是管道加熱器，當為電加熱器時，該電加熱器係採用電熱絲、電熱管或電熱片之其中任一種，而為管道加熱器時，該管道加熱器係採用氣體燃料或液體燃料之其中任一種。而該熱氣輸送管路45的一端係與該吸附轉輪40之脫附區403的另一側連接，且該吸附轉輪40之脫附區403的一側係與該脫附濃縮氣體管路46的一端連接，使將經由該第二加熱器50所提升之熱氣透過該熱氣輸送管路45來傳輸到該吸附轉輪40之脫附區403來進行脫附使用，並將經過高溫所脫附下來的脫附濃縮氣體透過該脫附濃縮氣體管路46來傳輸運送。另該脫附濃縮氣體管路46係設有一風車461，以將該脫附濃縮氣體管路46內的脫附濃縮氣體進行抽送。 In addition, one end of the cooling gas delivery pipeline 44 is connected to the other side of the cooling zone 402 of the adsorption rotor 40, and the other end of the cooling gas delivery pipeline 44 is connected to the second heater 50, and the The other end of the second heater 50 is connected to the other end of the hot gas conveying pipe 45 (as shown in Figures 6 to 8), wherein the second heater 50 is an electric heater or a pipe heater When it is an electric heater, the electric heater adopts any one of electric heating wire, electric heating tube or electric heating sheet, and when it is a pipeline heater, the pipeline heater adopts either gas fuel or liquid fuel. One end of the hot gas transport pipeline 45 is connected to the other side of the desorption zone 403 of the adsorption runner 40, and one side of the desorption zone 403 of the adsorption runner 40 is connected to the desorption concentrated gas pipeline. One end of 46 is connected, so that the hot gas lifted by the second heater 50 is transmitted through the hot gas delivery pipe 45 to the desorption zone 403 of the adsorption rotor 40 for desorption use, and will be desorbed after high temperature. The attached desorbed concentrated gas is transported through the desorbed concentrated gas pipeline 46. In addition, the desorbed concentrated gas pipeline 46 is provided with a windmill 461 to pump the desorbed concentrated gas in the desorbed concentrated gas pipeline 46.

另本發明第二種實施方式中的該冷卻氣輸送管路44與該熱氣輸送管路45之間係設有比例風門，而該比例風門係設有兩種實施設計，其中第一種實施設計乃為該冷卻氣輸送管路44與該熱氣輸送管路45之間設有一連通管路47，且該連通管路47係設有一連通控制閥門471，而該熱氣輸送管路45係設有一熱氣控制閥門451(如第7圖所示)，並透過該連通控制閥門471及該熱氣控制閥門451來形成比例風門，另第二實施設計乃為該冷卻氣輸送管路44與該熱氣輸送管路45之間設有一連通管路47，且該連通管路47係設有一連通控制閥門471，而該冷卻氣輸送管路44係設有一冷卻氣控制閥門441(如第8圖所示)，並透過該連通控制閥門471及該冷卻氣控制閥門441來形成比例風門，藉此，不管是透過該連通控制閥門471及該熱氣控制閥門451之設計的比例風門或是透過該連通控制閥門471及該冷卻氣控制閥門441之設計的比例風門，皆能調整控制風力之大小，讓該熱氣輸送管路45內的溫度保持一定高溫來提供給該吸附轉輪40之脫附區403使用。 In addition, in the second embodiment of the present invention, a proportional damper is provided between the cooling gas delivery pipe 44 and the hot gas delivery pipe 45, and the proportional damper is provided with two implementation designs, of which the first implementation design A communicating pipe 47 is provided between the cooling gas conveying pipe 44 and the hot gas conveying pipe 45, and the communicating pipe 47 is provided with a communicating control valve 471, and the hot gas conveying pipe 45 is provided with There is a hot gas control valve 451 (as shown in Figure 7), and a proportional damper is formed through the communication control valve 471 and the hot gas control valve 451. Another second implementation design is for the cooling gas delivery pipeline 44 and the hot gas delivery A connecting pipeline 47 is provided between the pipelines 45, and the connecting pipeline 47 is provided with a connecting control valve 471, and the cooling gas delivery pipeline 44 is provided with a cooling gas control valve 441 (as shown in Figure 8 Show), and through the communication control valve 471 and the cooling gas control valve 441 to form a proportional damper, thereby, whether through the communication control valve 471 and the hot gas control valve 451 design proportional damper or through the communication control Both the valve 471 and the proportional damper designed for the cooling gas control valve 441 can adjust and control the size of the wind force, so that the temperature in the hot gas conveying pipe 45 can be maintained at a certain high temperature to be used by the desorption zone 403 of the adsorption rotor 40 .

另該第二熱交換器70係連接有一第二脫附濃縮氣體輸送管路71及一第二熱氣回收管路72(如第6圖至第8圖所示)，該第二熱交換器70之第二冷側管路701的一端係與該脫附濃縮氣體管路46的另一端連接，該第二脫附濃縮氣體輸送管路71的一端係與該第二熱交換器70之第二冷側管路701的另一端連接，該第二脫附濃縮氣體輸送管路71的另一端係與該第一加熱器30之一端連接，該第二熱氣回收管路72的一端係與該第二熱交換器70之第二熱側管路702的一端連接，該第二熱氣回收管路72的另一端係與該廢氣進氣管路41連接。 In addition, the second heat exchanger 70 is connected to a second desorption concentrated gas delivery pipe 71 and a second hot gas recovery pipe 72 (as shown in Figs. 6 to 8). The second heat exchanger 70 One end of the second cold-side pipeline 701 is connected to the other end of the desorption concentrated gas pipeline 46, and one end of the second desorption concentrated gas delivery pipeline 71 is connected to the second end of the second heat exchanger 70 The other end of the cold side pipeline 701 is connected, the other end of the second desorption concentrated gas delivery pipeline 71 is connected to one end of the first heater 30, and one end of the second hot gas recovery pipeline 72 is connected to the first heater 30. One end of the second hot side pipeline 702 of the second heat exchanger 70 is connected, and the other end of the second hot gas recovery pipeline 72 is connected to the exhaust gas inlet pipeline 41.

而上述之第二脫附濃縮氣體輸送管路71的另一端所連接的第一加熱器30係為電加熱器或是管道加熱器，當為電加熱器時，該電加熱器係採用電熱絲、電熱管或電熱片之其中任一種，而為管道加熱器時，該管道加熱器係採用氣體燃料或液體燃料之其中任一種。另該第一加熱器30係設有一第一加熱器輸送管路31(如第6圖至第8圖所示)，該第一加熱器輸送管路31之另一端係與該吸附反應床20之一端連接，其中該吸附反應床20係設有一吸附反應床輸送管路21(如第6圖至第8圖所示)，該吸附反應床輸送管路21之另一端係與該觸媒床10之進氣口11連接(如第6圖至第8圖所示)，而該吸附反應床20係為具多孔之材質，以用將含矽的有機化合物進行反應成為二氧化矽(SiO2)等微粒並吸附。 The first heater 30 connected to the other end of the second desorption concentrated gas delivery pipeline 71 is an electric heater or a pipeline heater. When it is an electric heater, the electric heater uses an electric heating wire. , Electric heating tube or electric heating fin, and when it is a pipeline heater, the pipeline heater uses either gas fuel or liquid fuel. In addition, the first heater 30 is provided with a first heater delivery pipe 31 (as shown in Figures 6 to 8), and the other end of the first heater delivery pipe 31 is connected to the adsorption reaction bed 20 One end is connected, wherein the adsorption reaction bed 20 is provided with an adsorption reaction bed conveying pipeline 21 (as shown in Figs. 6 to 8), and the other end of the adsorption reaction bed conveying pipeline 21 is connected to the catalyst bed The air inlet 11 of 10 is connected (as shown in Fig. 6 to Fig. 8), and the adsorption reaction bed 20 is made of porous material to react organic compounds containing silicon into silicon dioxide (SiO 2 ) Wait for particles and adsorb.

再者，該冷卻器80係設有冷卻水管路801(如第6圖至第8圖所示)，以一進一出的方式來將流經該冷卻器80的高溫熱氣進行降溫，且該冷卻器80係為殼管式冷卻器、鰭管式冷卻器或板式熱交換器冷卻器之其中任一，且該冷卻器80係連接有一冷卻熱氣回收管路81及一觸媒床熱氣回收管路82(如第6圖至第8圖所示)，其中該觸媒床熱氣回收管路82的另一端係與該觸媒床10之出氣口12連接，以將由該觸媒床10之出氣口12所流出的高溫熱氣來輸送到該冷卻器80中，另該冷卻熱氣回收管路81的另一端係與該第二熱交換器70之第二熱側管路702的另一端連接，以將經過冷卻器80降溫過的高溫熱氣再輸送到該第二熱交換器70內。 Furthermore, the cooler 80 is provided with a cooling water pipeline 801 (as shown in Figures 6 to 8) to cool the high temperature hot air flowing through the cooler 80 in a one-in-one-out manner, and the cooling The device 80 is any one of a shell and tube cooler, a fin-tube cooler or a plate heat exchanger cooler, and the cooler 80 is connected with a cooling hot gas recovery line 81 and a catalyst bed hot gas recovery line 82 (as shown in Figures 6 to 8), wherein the other end of the catalyst bed hot gas recovery pipeline 82 is connected to the gas outlet 12 of the catalyst bed 10 to connect the gas outlet of the catalyst bed 10 12 The high-temperature hot gas flowing out is delivered to the cooler 80, and the other end of the cooling hot gas recovery pipe 81 is connected to the other end of the second hot side pipe 702 of the second heat exchanger 70 to connect The high-temperature hot air cooled by the cooler 80 is then sent to the second heat exchanger 70.

而本發明係於該第二熱交換器70之第二熱氣回收管路72上係設有一除塵設備721(如第7圖所示)，該除塵設備721係為袋式 除塵器、電袋式複合除塵器、慣性除塵器、靜電除塵器、離心式除塵器、濾筒式脈衝除塵器、脈衝袋式除塵器、脈衝濾芯除塵器、脈衝噴吹袋式除塵器、濕式除塵器、濕式電除塵器、濕式靜電除塵器、水膜除塵器、文丘里管除塵器、旋風分離器、煙道除塵器、多層除塵器、負壓反吹濾袋除塵器、低壓長袋脈衝除塵器、臥式靜電除塵器、無動力除塵器、荷電水霧除塵器、多管旋風除塵器、防爆除塵器之其中任一，或是於該第二熱交換器70之第二熱氣回收管路72設有一濾網裝置722(如第8圖所示)，透過該除塵設備721或是該濾網裝置722來將要進入該廢氣進氣管路41的熱氣先進行除塵或過濾。 In the present invention, a dust removal device 721 (as shown in Figure 7) is provided on the second hot gas recovery pipe 72 of the second heat exchanger 70, and the dust removal device 721 is a bag type Dust collector, electric bag composite dust collector, inertial dust collector, electrostatic precipitator, centrifugal dust collector, filter cartridge pulse dust collector, pulse bag filter, pulse filter dust collector, pulse jet bag filter, wet Type dust collector, wet electrostatic precipitator, wet electrostatic precipitator, water film dust collector, venturi tube dust collector, cyclone separator, flue dust collector, multi-layer dust collector, negative pressure back blow filter bag dust collector, low pressure Long bag pulse dust collector, horizontal electrostatic dust collector, unpowered dust collector, charged water mist dust collector, multi-tube cyclone dust collector, explosion-proof dust collector, or the second heat exchanger 70 The hot gas recovery pipeline 72 is provided with a filter device 722 (as shown in FIG. 8 ), through the dust removal equipment 721 or the filter device 722, the hot gas entering the exhaust gas inlet pipe 41 is first dedusted or filtered.

藉此，讓該吸附轉輪40之脫附區403所脫附下來的脫附濃縮氣體透過該脫附濃縮氣體管路46來傳輸到該第二熱交換器70之第二冷側管路701來進行熱交換，並再透過該第二脫附濃縮氣體輸送管路71來傳輸到該第一加熱器30中，讓該第一加熱器30來將所輸送過來脫附濃縮氣體進行加熱以提高脫附濃縮氣體之溫度，再將提高溫度之脫附濃縮氣體透過該第一加熱器送管路31來輸送至該吸附反應床20，使該吸附反應床20將含矽的有機化合物進行反應成為二氧化矽(SiO2)等微粒並吸附，再由該吸附反應床輸送管路21來輸送到觸媒床10內進行處理。 Thereby, the desorbed concentrated gas desorbed from the desorption zone 403 of the adsorption rotor 40 is transmitted to the second cold side pipe 701 of the second heat exchanger 70 through the desorbed concentrated gas pipe 46 To carry out heat exchange, and then transmit it to the first heater 30 through the second desorption concentrated gas delivery pipe 71, and let the first heater 30 heat the delivered desorption concentrated gas to improve The temperature of the desorbed concentrated gas, and then the desorbed concentrated gas with an increased temperature is sent to the adsorption reaction bed 20 through the first heater delivery pipe 31, so that the adsorption reaction bed 20 reacts the organic compound containing silicon into Particles such as silicon dioxide (SiO 2 ) are adsorbed and transported to the catalyst bed 10 through the adsorption reaction bed transport pipeline 21 for processing.

當該觸媒床10進行處理後，即透過與該觸媒床10之出氣口12所連接的觸媒床熱氣回收管路82來將該觸媒床10處理之熱氣回收到該冷卻器80內，再透過該冷卻熱氣回收管路81來輸送到該第二熱交換器70之第二熱側管路702內進行熱交換，且再經由該第二熱氣回收管路72來輸送到該廢氣進氣管路41內，使經過該觸媒床10處理之 氣體進入該吸附轉輪40之吸附區401循環利用，而不經過該煙囪90來進行排放，讓該煙囪90的排放量降低，並使有機廢氣的處理效率提升。 After the catalyst bed 10 is processed, the hot gas from the catalyst bed 10 is recovered into the cooler 80 through the catalyst bed hot gas recovery pipeline 82 connected to the outlet 12 of the catalyst bed 10 , And then transported to the second hot side pipe 702 of the second heat exchanger 70 through the cooling hot gas recovery line 81 for heat exchange, and then transported to the exhaust gas inlet through the second hot gas recovery line 72 In the gas pipeline 41, the catalyst bed 10 The gas enters the adsorption zone 401 of the adsorption rotor 40 for recycling without passing through the chimney 90 for discharge, so that the emission of the chimney 90 is reduced and the treatment efficiency of organic waste gas is improved.

再者，本發明第二種實施方式的觸媒回流高效率有機廢氣處理方法，其主要係用於有機廢氣處理系統，係包括有一觸媒床10、一吸附反應床20、一第一加熱器30、一吸附轉輪40、一第二加熱器50、一第二熱交換器70及一冷卻器80，該吸附轉輪40係設有吸附區401、冷卻區402及脫附區403，該吸附轉輪40係連接有一廢氣進氣管路41、一淨氣排放管路42、一冷卻氣進氣管路43、一冷卻氣輸送管路44、一熱氣輸送管路45及一脫附濃縮氣體管路46，該第二熱交換器70係設有第二冷側管路701及第二熱側管路702(如第6圖至第8圖所示)，該第二熱交換器70係連接有一第二脫附濃縮氣體輸送管路71及一第二熱氣回收管路72，該第一加熱器30係設有一第一加熱器輸送管路31，該吸附反應床20係設有一吸附反應床輸送管路21，該冷卻器80係設有冷卻水管路801，該冷卻器80係連接有一冷卻熱氣回收管路81及一觸媒床熱氣回收管路82。 Furthermore, the catalyst refluxing high-efficiency organic waste gas treatment method of the second embodiment of the present invention is mainly used in an organic waste gas treatment system, and includes a catalyst bed 10, an adsorption reaction bed 20, and a first heater 30. An adsorption runner 40, a second heater 50, a second heat exchanger 70 and a cooler 80. The adsorption runner 40 is provided with an adsorption zone 401, a cooling zone 402, and a desorption zone 403. The adsorption runner 40 is connected to an exhaust gas inlet pipe 41, a clean gas discharge pipe 42, a cooling gas inlet pipe 43, a cooling gas delivery pipe 44, a hot gas delivery pipe 45 and a desorption concentration A gas pipeline 46, the second heat exchanger 70 is provided with a second cold side pipeline 701 and a second hot side pipeline 702 (as shown in Figures 6 to 8), the second heat exchanger 70 A second desorption concentrated gas delivery pipeline 71 and a second hot gas recovery pipeline 72 are connected, the first heater 30 is provided with a first heater delivery pipeline 31, and the adsorption reaction bed 20 is provided with an adsorption The reaction bed conveying pipeline 21, the cooler 80 is provided with a cooling water pipeline 801, and the cooler 80 is connected with a cooling hot gas recovery pipeline 81 and a catalyst bed hot gas recovery pipeline 82.

而該處理方法的主要步驟(如第5圖所示)係包括：步驟S200吸附區吸附：將廢氣透過該廢氣進氣管路41的另一端來送入該吸附轉輪40之吸附區401的一側進行吸附，再將吸附後之氣體透過該淨氣排放管路42的另一端來進行輸送。而完成上述步驟S200後即進行下一步驟S210。 The main steps of the treatment method (as shown in Figure 5) include: step S200 adsorption zone adsorption: the exhaust gas is sent to the adsorption zone 401 of the adsorption rotor 40 through the other end of the exhaust gas inlet pipe 41 One side is adsorbed, and the adsorbed gas is transmitted through the other end of the clean gas discharge pipeline 42. After the above step S200 is completed, the next step S210 is performed.

其中上述之步驟S200中該淨氣排放管路42的另一端係連接一煙囪90(如第6圖至第8圖所示)，讓經由該淨氣排放管路42所 排出淨化後氣體輸送到煙囪90來進行排放。另該淨氣排放管路42係設有一風車421(如第7圖及第8圖所示)，以將該淨氣排放管路42內的氣體推向該煙囪90。 In the above step S200, the other end of the clean gas discharge pipeline 42 is connected to a chimney 90 (as shown in Figures 6 to 8), so that the clean gas discharge pipeline 42 The purified gas is sent to the chimney 90 for discharge. In addition, the clean gas discharge pipeline 42 is provided with a windmill 421 (as shown in FIGS. 7 and 8) to push the gas in the clean gas discharge pipeline 42 toward the chimney 90.

另，下一步進行的步驟S210冷卻區冷卻：透過該冷卻氣進氣管路43的另一端來輸送冷卻氣至該吸附轉輪40之冷卻區402進行冷卻，再透過該冷卻氣輸送管路44的另一端來將經過冷卻區402之冷卻氣輸送到該第二加熱器50內。而完成上述步驟S210後即進行下一步驟S220。 In addition, the next step S210 cooling zone cooling: the cooling air is delivered to the cooling zone 402 of the adsorption runner 40 through the other end of the cooling air inlet pipe 43 for cooling, and then the cooling air delivery pipe 44 The other end of the cooling zone 402 is used to deliver the cooling air to the second heater 50. After the above step S210 is completed, the next step S220 is performed.

其中該上述之步驟S210中該第二加熱器50係為電加熱器或是管道加熱器，當為電加熱器時，該電加熱器係採用電熱絲、電熱管或電熱片之其中任一種，而為管道加熱器時，該管道加熱器係採用氣體燃料或液體燃料之其中任一種。另該冷卻氣進氣管路43的一端係與該吸附轉輪40之冷卻區402的一側連接，而該冷卻氣進氣管路43係有兩種實施態樣，其中第一種實施態樣為該冷卻氣進氣管路43乃是供外氣進入(如第6圖及第7圖所示)，而該外氣係為新鮮空氣，以將該外氣用來輸送到該吸附轉輪40之冷卻區402內提供降溫使用，另第二種實施態樣係該冷卻氣進氣管路43係設有一氣體旁通管路431(如第8圖所示)，該氣體旁通管路431之一端係與該冷卻氣進氣管路43連接，而該氣體旁通管路431之另一端係與該廢氣進氣管路41連接，透過該氣體旁通管路431來將部份的廢氣輸送到該吸附轉輪40之冷卻區402內提供降溫使用。 Wherein the second heater 50 in the above step S210 is an electric heater or a pipe heater. When it is an electric heater, the electric heater uses any one of an electric heating wire, an electric heating tube or an electric heating sheet, In the case of a pipeline heater, the pipeline heater uses either gas fuel or liquid fuel. In addition, one end of the cooling gas intake pipe 43 is connected to one side of the cooling zone 402 of the adsorption runner 40, and the cooling gas intake pipe 43 has two implementation modes, the first one is So the cooling air intake pipe 43 is for external air to enter (as shown in Figure 6 and Figure 7), and the external air system is fresh air to transport the external air to the adsorption converter The cooling area 402 of the wheel 40 is used for cooling. Another second embodiment is that the cooling gas inlet pipe 43 is provided with a gas bypass pipe 431 (as shown in Figure 8). The gas bypass pipe One end of the path 431 is connected to the cooling gas inlet pipe 43, and the other end of the gas bypass pipe 431 is connected to the exhaust gas inlet pipe 41. Part of the gas bypass pipe 431 The exhaust gas is transported to the cooling zone 402 of the adsorption rotor 40 for cooling.

另，下一步進行的步驟S220脫附區脫附：透過與該第二 加熱器50的另一端所連接的熱氣輸送管路45來將熱氣體輸送到該吸附轉輪40之脫附區403進行脫附，再透過該脫附濃縮氣體管路46的另一端來將脫附濃縮氣體輸送到第二熱交換器70之第二冷側管路702的一端。而完成上述步驟S220後即進行下一步驟S230。 In addition, the next step S220 desorption zone desorption: through the second The hot gas delivery pipe 45 connected to the other end of the heater 50 transports the hot gas to the desorption zone 403 of the adsorption rotor 40 for desorption, and then desorbs it through the other end of the desorption concentrated gas pipe 46 The concentrated gas is delivered to one end of the second cold side pipeline 702 of the second heat exchanger 70. After the above step S220 is completed, the next step S230 is performed.

其中該上述之步驟S220中該脫附濃縮氣體管路46係設有一風車461，以將該脫附濃縮氣體管路46內的脫附濃縮氣體進行抽送。另該冷卻氣輸送管路44與該熱氣輸送管路45之間係設有比例風門，而該比例風門係設有兩種實施設計，其中第一種實施設計乃為該冷卻氣輸送管路44與該熱氣輸送管路45之間設有一連通管路47，且該連通管路47係設有一連通控制閥門471，而該熱氣輸送管路45係設有一熱氣控制閥門451(如第7圖所示)，並透過該連通控制閥門471及該熱氣控制閥門451來形成比例風門。另第二實施設計乃為該冷卻氣輸送管路44與該熱氣輸送管路45之間設有一連通管路47，且該連通管路47係設有一連通控制閥門471，而該冷卻氣輸送管路44係設有一冷卻氣控制閥門441(如第8圖所示)，並透過該連通控制閥門471及該冷卻氣控制閥門441來形成比例風門。藉此，不管是透過該連通控制閥門471及該熱氣控制閥門451之設計的比例風門或是透過該連通控制閥門471及該冷卻氣控制閥門441之設計的比例風門，皆能調整控制風力之大小，讓該熱氣輸送管路45內的溫度保持一定高溫來提供給該吸附轉輪40之脫附區403使用。 In the step S220 described above, the desorbed concentrated gas pipeline 46 is provided with a windmill 461 to pump the desorbed concentrated gas in the desorbed concentrated gas pipeline 46. In addition, a proportional damper is provided between the cooling gas conveying pipeline 44 and the hot gas conveying pipeline 45, and the proportional damper is provided with two implementation designs. The first implementation design is the cooling gas delivery pipeline 44 A connecting pipeline 47 is provided with the hot gas delivery pipeline 45, and the connecting pipeline 47 is provided with a connecting control valve 471, and the hot gas delivery pipeline 45 is provided with a hot gas control valve 451 (e.g. As shown in the figure), a proportional damper is formed through the communication control valve 471 and the hot gas control valve 451. Another second implementation design is that a communicating pipe 47 is provided between the cooling gas conveying pipe 44 and the hot gas conveying pipe 45, and the communicating pipe 47 is provided with a communicating control valve 471, and the cooling gas The conveying pipeline 44 is provided with a cooling gas control valve 441 (as shown in FIG. 8), and a proportional damper is formed through the communication control valve 471 and the cooling gas control valve 441. Thereby, regardless of the proportional damper designed through the communication control valve 471 and the hot gas control valve 451 or the proportional damper designed through the communication control valve 471 and the cooling gas control valve 441, the magnitude of the control wind can be adjusted. , Keep the temperature in the hot gas conveying pipeline 45 at a certain high temperature to provide the desorption zone 403 of the adsorption rotor 40 for use.

另，下一步進行的步驟S230脫附濃縮氣體輸送：該脫附濃縮氣體再透過該第二熱交換器70之第二冷側管路701的另一端所連 接的第二脫附濃縮氣體輸送管路71來輸送到該第一加熱器30內。而完成上述步驟S230後即進行下一步驟S240。 In addition, the next step S230 desorption concentrated gas transportation: the desorption concentrated gas then passes through the second heat exchanger 70 connected to the other end of the second cold side pipeline 701 The connected second desorption concentrated gas delivery pipeline 71 is delivered to the first heater 30. After the above step S230 is completed, the next step S240 is performed.

其中該上述之步驟S230中該第一加熱器30係為電加熱器或是管道加熱器，當為電加熱器時，該電加熱器係採用電熱絲、電熱管或電熱片之其中任一種，而為管道加熱器時，該管道加熱器係採用氣體燃料或液體燃料之其中任一種。 In the above step S230, the first heater 30 is an electric heater or a pipe heater. When it is an electric heater, the electric heater uses any one of an electric heating wire, an electric heating tube or an electric heating fin, In the case of a pipeline heater, the pipeline heater uses either gas fuel or liquid fuel.

另，下一步進行的步驟S240吸附反應床吸附：將經由該第一加熱器30進行加熱升溫的脫附濃縮氣體透過該第一加熱器輸送管路31來輸送至該吸附反應床20來進行吸附，其中該吸附反應床20係為具多孔之材質，以用來將含矽的有機化合物進行反應成為二氧化矽(SiO2)等微粒並吸附。而完成上述步驟S240後即進行下一步驟S250。 In addition, the next step S240 adsorption reaction bed adsorption: the desorption concentrated gas heated by the first heater 30 is sent to the adsorption reaction bed 20 through the first heater delivery pipe 31 for adsorption. Wherein, the adsorption reaction bed 20 is made of a porous material for reacting organic compounds containing silicon into particles such as silicon dioxide (SiO 2 ) and adsorbing them. After the above step S240 is completed, the next step S250 is performed.

另，下一步進行的步驟S250觸媒床處理：將經過該吸附反應床20進行吸附的脫附濃縮氣體再透過該吸附反應床輸送管路21來輸送到觸媒床10內進行處理。而完成上述步驟S250後即進行下一步驟S260。 In addition, the next step S250 catalyst bed treatment: the desorption concentrated gas that has been adsorbed by the adsorption reaction bed 20 is transported to the catalyst bed 10 through the adsorption reaction bed delivery pipeline 21 for processing. After the above step S250 is completed, the next step S260 is performed.

另，下一步進行的步驟S260觸媒床氣體輸送：將經過觸媒床10處理後之氣體透過該觸媒床10之出氣口12所連接的觸媒床熱氣回收管路82輸送到該冷卻器80內，再由該冷卻器80之另一端所連接的冷卻熱氣回收管路81輸送到該第二熱交換器70之第二熱側管路702的一端。而完成上述步驟S260後即進行下一步驟S270。 In addition, the next step S260 catalyst bed gas transportation: the gas after the catalyst bed 10 is transported to the cooler through the catalyst bed hot gas recovery pipeline 82 connected to the gas outlet 12 of the catalyst bed 10 In 80, the cooling hot gas recovery pipe 81 connected to the other end of the cooler 80 is transported to one end of the second hot side pipe 702 of the second heat exchanger 70. After the above step S260 is completed, the next step S270 is performed.

其中該上述之步驟S260中該冷卻器80係設有冷卻水管路801(如第6圖至第8圖所示)，以一進一出的方式來將流經該冷卻器 80的高溫熱氣進行降溫，且該冷卻器80係為殼管式冷卻器、鰭管式冷卻器或板式熱交換器冷卻器之其中任一。 In the above step S260, the cooler 80 is provided with a cooling water pipe 801 (as shown in Figures 6 to 8), which will flow through the cooler in a way of one in and one out. The high-temperature hot air 80 is cooled, and the cooler 80 is any one of a shell and tube cooler, a fin tube cooler, or a plate heat exchanger cooler.

另，下一步進行的步驟S270觸媒床氣體回收輸送：將輸送到該第二熱交換器70之第二熱側管路702的觸媒床10之氣體，再經由與該第二熱交換器70之第二熱側管路702的另一端所連接的第二熱氣回收管路72來輸送到該廢氣進氣管路41連接。 In addition, the next step S270 is the catalyst bed gas recovery and transportation: the gas that is transported to the catalyst bed 10 of the second hot side pipeline 702 of the second heat exchanger 70 is passed through the second heat exchanger The second hot gas recovery pipe 72 connected to the other end of the second hot side pipe 702 of 70 is connected to the exhaust gas intake pipe 41.

其中該上述之步驟S270中該第二熱交換器70之第二熱氣回收管路72上係設有一除塵設備721(如第7圖所示)，該除塵設備721係為袋式除塵器、電袋式複合除塵器、慣性除塵器、靜電除塵器、離心式除塵器、濾筒式脈衝除塵器、脈衝袋式除塵器、脈衝濾芯除塵器、脈衝噴吹袋式除塵器、濕式除塵器、濕式電除塵器、濕式靜電除塵器、水膜除塵器、文丘里管除塵器、旋風分離器、煙道除塵器、多層除塵器、負壓反吹濾袋除塵器、低壓長袋脈衝除塵器、臥式靜電除塵器、無動力除塵器、荷電水霧除塵器、多管旋風除塵器、防爆除塵器之其中任一，或是於該第二熱交換器70之第二熱氣回收管路72設有一濾網裝置722(如第8圖所示)，透過該除塵設備721或是該濾網裝置722來將要進入該廢氣進氣管路41的熱氣先進行除塵或過濾。 In the above step S270, the second hot gas recovery pipeline 72 of the second heat exchanger 70 is provided with a dust removal device 721 (as shown in Figure 7), and the dust removal device 721 is a bag filter, an electric Bag type composite dust collector, inertial dust collector, electrostatic dust collector, centrifugal dust collector, filter cartridge pulse dust collector, pulse bag filter, pulse filter dust collector, pulse jet bag dust collector, wet dust collector, Wet electrostatic precipitator, wet electrostatic precipitator, water film dust collector, venturi dust collector, cyclone separator, flue dust collector, multi-layer dust collector, negative pressure back blow filter bag dust collector, low pressure long bag pulse dust collector Any one of the filter, horizontal electrostatic precipitator, unpowered precipitator, charged water mist precipitator, multi-tube cyclone precipitator, explosion-proof precipitator, or the second hot gas recovery pipeline in the second heat exchanger 70 72 is provided with a filter device 722 (as shown in FIG. 8), through the dust removal equipment 721 or the filter device 722, the hot air entering the exhaust gas inlet pipe 41 is first dusted or filtered.

藉此，讓該吸附轉輪40之脫附區403所脫附下來的脫附濃縮氣體透過該脫附濃縮氣體管路46來傳輸到該第二熱交換器70之第二冷側管路701來進行熱交換，並再透過該第二脫附濃縮氣體輸送管路71來傳輸到該第一加熱器30中，讓該第一加熱器30來將所輸送過來脫附濃縮氣體進行加熱以提高脫附濃縮氣體之溫度，再將提高溫度之脫附 濃縮氣體透過該第一加熱器送管路31來輸送至該吸附反應床20，使該吸附反應床20將含矽的有機化合物進行反應成為二氧化矽(SiO2)等微粒並吸附，再由該吸附反應床輸送管路21來輸送到觸媒床10內進行處理。 Thereby, the desorbed concentrated gas desorbed from the desorption zone 403 of the adsorption rotor 40 is transmitted to the second cold side pipe 701 of the second heat exchanger 70 through the desorbed concentrated gas pipe 46 To carry out heat exchange, and then transmit it to the first heater 30 through the second desorption concentrated gas delivery pipe 71, and let the first heater 30 heat the delivered desorption concentrated gas to improve The temperature of the desorbed concentrated gas, and then the desorbed concentrated gas with an increased temperature is sent to the adsorption reaction bed 20 through the first heater delivery pipe 31, so that the adsorption reaction bed 20 reacts the organic compound containing silicon into Particles such as silicon dioxide (SiO 2 ) are adsorbed and transported to the catalyst bed 10 through the adsorption reaction bed transport pipeline 21 for processing.

當該觸媒床10進行處理後，即透過與該觸媒床10之出氣口12所連接的觸媒床熱氣回收管路82來將該觸媒床10處理之熱氣回收到該冷卻器80內，再透過該冷卻熱氣回收管路81來輸送到該第二熱交換器70之第二熱側管路702內進行熱交換，且再經由該第二熱氣回收管路72來輸送到該廢氣進氣管路41內，使經過該觸媒床10處理之氣體進入該吸附轉輪40之吸附區401循環利用，而不經過該煙囪90來進行排放，讓該煙囪90的排放量降低，並使有機廢氣的處理效率提升。 After the catalyst bed 10 is processed, the hot gas from the catalyst bed 10 is recovered into the cooler 80 through the catalyst bed hot gas recovery pipeline 82 connected to the outlet 12 of the catalyst bed 10 , And then transported to the second hot side pipe 702 of the second heat exchanger 70 through the cooling hot gas recovery line 81 for heat exchange, and then transported to the exhaust gas inlet through the second hot gas recovery line 72 In the gas pipeline 41, the gas processed by the catalyst bed 10 enters the adsorption zone 401 of the adsorption rotor 40 for recycling, instead of passing through the chimney 90 for discharge, so that the emission of the chimney 90 is reduced, and The treatment efficiency of organic waste gas is improved.

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。 Based on the above detailed description, those who are familiar with this technique can understand that the present invention can indeed achieve the aforementioned objects, and that it has actually complied with the provisions of the Patent Law, and filed an application for a patent for invention.

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 preferred embodiments of the present invention, and should not be used to limit the scope of implementation of the present invention; therefore, all simple equivalent changes and modifications made in accordance with the scope of the patent application of the present invention and the content of the description of the invention , Should still fall within the scope of the invention patent.

S100‧‧‧吸附區吸附 S100‧‧‧Adsorption zone adsorption

S110‧‧‧冷卻區冷卻 S110‧‧‧Cooling area cooling

S120‧‧‧脫附區脫附 S120‧‧‧Desorption zone desorption

S130‧‧‧脫附濃縮氣體輸送 S130‧‧‧Desorption concentrated gas delivery

S140‧‧‧吸附反應床吸附 S140‧‧‧Adsorption reaction bed adsorption

S150‧‧‧觸媒床處理 S150‧‧‧Catalyst bed treatment

S160‧‧‧觸媒床氣體輸送 S160‧‧‧Catalyst bed gas delivery

S170‧‧‧觸媒床氣體回收輸送 S170‧‧‧Catalyst bed gas recovery and transportation

Claims (26)

一種觸媒回流高效率有機廢氣處理系統，係包括：一觸媒床，該觸媒床係設有一進氣口及一出氣口；一吸附反應床，該吸附反應床係設有一吸附反應床輸送管路，該吸附反應床輸送管路之另一端係與該觸媒床之進氣口連接；一第一加熱器，該第一加熱器係設有一第一加熱器輸送管路，該第一加熱器輸送管路之另一端係與該吸附反應床之一端連接；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，該廢氣進氣管路的另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的一側連接，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；一第二加熱器，該第二加熱器的一端係與該冷卻氣輸送管路的另一端連接，該第二加熱器的另一端係與該熱氣輸送管路的另一端連接；一第一熱交換器，該第一熱交換器係設有第一冷側管路及第一熱側管路，該第一熱交換器係連接有一第一熱氣回收管路、一第一觸媒床熱氣回收管路及一第一脫附濃縮氣體輸送管路，該第一觸媒床熱氣回收管路的一端係與該第一熱側管路的一端連接，該第一觸媒床熱氣回收管路的 另一端係與該觸媒床之出氣口連接，該第一熱氣回收管路的一端係與該第一熱側管路的另一端連接，該第一脫附濃縮氣體輸送管路的一端係與該第一冷側管路的另一端連接，該第一脫附濃縮氣體輸送管路的另一端係與該第一加熱器之一端連接；以及一第二熱交換器，該第二熱交換器係設有第二冷側管路及第二熱側管路，該第二熱交換器係連接有一第二脫附濃縮氣體輸送管路及一第二熱氣回收管路，該第二冷側管路的一端係與該脫附濃縮氣體管路的另一端連接，該第二脫附濃縮氣體輸送管路的一端係與該第二冷側管路的另一端連接，該第二脫附濃縮氣體輸送管路的另一端係與該第一冷側管路的一端連接，該第二熱氣回收管路的一端係與該第二熱側管路的一端連接，該第二熱氣回收管路的另一端係與該廢氣進氣管路連接，該第二熱側管路的另一端係與該第一熱氣回收管路的另一端連接。 A catalyst refluxing high-efficiency organic waste gas treatment system includes: a catalyst bed, the catalyst bed is provided with an air inlet and an air outlet; an adsorption reaction bed, the adsorption reaction bed is provided with an adsorption reaction bed for transportation Pipeline, the other end of the adsorption reaction bed delivery pipeline is connected to the gas inlet of the catalyst bed; a first heater is provided with a first heater delivery pipeline, the first The other end of the heater conveying pipeline is connected with one end of the adsorption reaction bed; an adsorption runner, the adsorption runner system is provided with an adsorption zone, a cooling zone and a desorption zone, and the adsorption runner system is connected with an exhaust gas inlet Pipeline, a clean gas discharge pipeline, a cooling gas inlet pipeline, a cooling gas delivery pipeline, a hot gas delivery pipeline and a desorption concentrated gas pipeline, the other end of the exhaust gas inlet pipeline is connected To one side of the adsorption zone of the adsorption runner, one end of the clean air discharge pipeline is connected to the other side of the adsorption zone of the adsorption runner, and one end of the cooling gas inlet pipeline is connected to the adsorption runner One side of the cooling zone is connected, one end of the cooling gas delivery pipeline is connected to the other side of the cooling zone of the adsorption runner, and one end of the hot gas delivery pipeline is connected to the other side of the desorption zone of the adsorption runner. One side is connected, one end of the desorption concentrated gas pipeline is connected to one side of the desorption zone of the adsorption runner; a second heater, one end of the second heater is connected to the cooling gas delivery pipeline The other end is connected, the other end of the second heater is connected to the other end of the hot gas conveying pipeline; a first heat exchanger is provided with a first cold side pipeline and a first heat Side pipeline, the first heat exchanger is connected with a first hot gas recovery pipeline, a first catalyst bed hot gas recovery pipeline and a first desorption concentrated gas delivery pipeline, the first catalyst bed hot gas recovery One end of the pipeline is connected to one end of the first hot side pipeline, and the first catalyst bed hot gas recovery pipeline The other end is connected to the gas outlet of the catalyst bed, one end of the first hot gas recovery pipeline is connected to the other end of the first hot side pipeline, and one end of the first desorption concentrated gas delivery pipeline is connected to The other end of the first cold side pipeline is connected, the other end of the first desorption concentrated gas delivery pipeline is connected to one end of the first heater; and a second heat exchanger, the second heat exchanger A second cold-side pipeline and a second hot-side pipeline are provided. The second heat exchanger is connected to a second desorption concentrated gas delivery pipeline and a second hot gas recovery pipeline. The second cold-side pipeline One end of the pipeline is connected with the other end of the desorption concentrated gas pipeline, one end of the second desorption concentrated gas delivery pipeline is connected with the other end of the second cold-side pipeline, the second desorption concentrated gas The other end of the conveying pipeline is connected to one end of the first cold side pipeline, one end of the second hot gas recovery pipeline is connected to one end of the second hot gas recovery pipeline, and the other end of the second hot gas recovery pipeline One end is connected with the exhaust gas intake pipeline, and the other end of the second hot side pipeline is connected with the other end of the first hot gas recovery pipeline. 一種觸媒回流高效率有機廢氣處理系統，係包括：一觸媒床，該觸媒床係設有一進氣口及一出氣口；一吸附反應床，該吸附反應床係設有一吸附反應床輸送管路，該吸附反應床輸送管路之另一端係與該觸媒床之進氣口連接；一第一加熱器，該第一加熱器係設有一第一加熱器輸送管路，該第一加熱器輸送管路之另一端係與該吸附反應床之一端連接；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，該廢氣進氣管路的另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的一側連接，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；一第二加熱器，該第二加熱器的一端係與該冷卻氣輸送管路的另一端連接，該第二加熱器的另一端係與該熱氣輸送管路的另一端連接；一第二熱交換器，該第二熱交換器係設有第二冷側管路及第二熱側管路，該第二熱交換器係連接有一第二脫附濃縮氣體輸送管路及一第二熱氣回收管路，該第二冷側管路的一端係與該脫附濃縮氣體管路的另一端連接，該第二脫附濃縮氣體輸送管路的一端係與該第二冷側管路的另一端連接，該第二脫附濃縮氣體輸送管路的另一端係與該第一加熱器之一端連接，該第二熱氣回收管路的一端係與該第二熱側管路的一端連接，該第二熱氣回收管路的另一端係與該廢氣進氣管路連接；以及一冷卻器，該冷卻器係設有冷卻水管路，該冷卻器係連接有一冷卻熱氣回收管路及一觸媒床熱氣回收管路，該觸媒床熱氣回收管路的另一端係與該觸媒床之出氣口連接，該冷卻熱氣回收管路的另一端係與該第二熱側管路的另一端連接。 A catalyst refluxing high-efficiency organic waste gas treatment system includes: a catalyst bed, the catalyst bed is provided with an air inlet and an air outlet; an adsorption reaction bed, the adsorption reaction bed is provided with an adsorption reaction bed for transportation Pipeline, the other end of the adsorption reaction bed delivery pipeline is connected to the gas inlet of the catalyst bed; a first heater is provided with a first heater delivery pipeline, the first The other end of the heater conveying pipeline is connected with one end of the adsorption reaction bed; an adsorption runner, the adsorption runner system is provided with an adsorption zone, a cooling zone and a desorption zone, and the adsorption runner system is connected with an exhaust gas inlet Pipeline, a clean gas discharge pipeline, a cooling gas inlet pipeline, a cooling gas delivery pipeline, a hot gas delivery pipeline and a desorption concentrated gas pipeline, the other end of the exhaust gas inlet pipeline is connected To one side of the adsorption zone of the adsorption runner, one of the clean gas discharge pipeline The end system is connected with the other side of the adsorption zone of the adsorption runner, one end of the cooling gas inlet pipe is connected with one side of the cooling zone 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, one end of the hot gas conveying pipeline is connected to the other side of the desorption zone of the adsorption runner, and one end of the desorption concentrated gas pipeline is connected to the adsorption runner One side of the desorption zone is connected; a second heater, one end of the second heater is connected to the other end of the cooling gas delivery pipeline, and the other end of the second heater is connected to the hot gas delivery pipeline The other end of the connection; a second heat exchanger, the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, the second heat exchanger is connected with a second desorption concentrated gas Delivery pipeline and a second hot gas recovery pipeline, one end of the second cold side pipeline is connected to the other end of the desorption concentrated gas pipeline, and one end of the second desorption concentrated gas delivery pipeline is connected to the The other end of the second cold-side pipeline is connected, the other end of the second desorption concentrated gas delivery pipeline is connected to one end of the first heater, and one end of the second hot gas recovery pipeline is connected to the second heater. One end of the side pipeline is connected, and the other end of the second hot gas recovery pipeline is connected to the exhaust gas intake pipeline; and a cooler, the cooler is provided with a cooling water pipeline, and the cooler is connected with a cooling hot gas The recovery pipeline and a catalyst bed hot gas recovery pipeline, the other end of the catalyst bed hot gas recovery pipeline is connected with the outlet of the catalyst bed, and the other end of the cooling hot gas recovery pipeline is connected with the second heat Connect the other end of the side pipe. 如申請專利範圍第1或2項所述之觸媒回流高效率有機廢氣處理系統，其中該第二熱交換器之第二熱氣回收管路係進一步設有一除塵設備，該除塵設備係為袋式除塵器、電袋式複合除塵器、慣性除塵器、靜電除塵器、離心式除塵器、濾筒式脈衝除塵器、脈衝袋式除塵器、脈衝 濾芯除塵器、脈衝噴吹袋式除塵器、濕式除塵器、濕式電除塵器、濕式靜電除塵器、水膜除塵器、文丘里管除塵器、旋風分離器、煙道除塵器、多層除塵器、負壓反吹濾袋除塵器、低壓長袋脈衝除塵器、臥式靜電除塵器、無動力除塵器、荷電水霧除塵器、多管旋風除塵器、防爆除塵器之其中任一。 For example, the catalyst recirculation high-efficiency organic waste gas treatment system described in item 1 or 2 of the scope of patent application, wherein the second hot gas recovery pipeline of the second heat exchanger is further provided with a dust removal device, which is a bag type Dust collector, electric bag type compound dust collector, inertial dust collector, electrostatic dust collector, centrifugal dust collector, filter cartridge pulse dust collector, pulse bag dust collector, pulse Filter element dust collector, pulse jet bag dust collector, wet dust collector, wet electric dust collector, wet electrostatic dust collector, water film dust collector, venturi tube dust collector, cyclone separator, flue dust collector, multi-layer Dust collector, negative pressure backflush filter bag dust collector, low pressure long bag pulse dust collector, horizontal electrostatic dust collector, unpowered dust collector, charged water mist dust collector, multi-tube cyclone dust collector, explosion-proof dust collector. 如申請專利範圍第1或2項所述之觸媒回流高效率有機廢氣處理系統，其中該第二熱交換器之第二熱氣回收管路係進一步設有一濾網裝置，該濾網裝置係用於進行除塵使用。 For example, the catalyst recirculation high-efficiency organic waste gas treatment system described in item 1 or 2 of the scope of patent application, wherein the second hot gas recovery pipeline of the second heat exchanger is further provided with a filter device, and the filter device is used Used for dust removal. 如申請專利範圍第1或2項所述之觸媒回流高效率有機廢氣處理系統，其中該第一加熱器及該第二加熱器係進一步分別為電加熱器，該電加熱器係採用電熱絲、電熱管或電熱片之其中任一種。 For example, the catalyst recirculation high-efficiency organic waste gas treatment system described in item 1 or 2 of the scope of patent application, wherein the first heater and the second heater are further respectively electric heaters, and the electric heater adopts electric heating wire , Either of electric heating tube or electric heating film. 如申請專利範圍第1或2項所述之觸媒回流高效率有機廢氣處理系統，其中該第一加熱器及該第二加熱器係進一步分別為管道加熱器，該管道加熱器係採用氣體燃料或液體燃料之其中任一種。 For example, the catalyst recirculation high-efficiency organic waste gas treatment system described in item 1 or 2 of the scope of patent application, wherein the first heater and the second heater are further pipeline heaters respectively, and the pipeline heater adopts gas fuel Or any of the liquid fuels. 如申請專利範圍第2項所述之觸媒回流高效率有機廢氣處理系統，其中該冷卻器係進一步為殼管式冷卻器、鰭管式冷卻器或板式熱交換器冷卻器之其中任一。 The catalyst reflux high-efficiency organic waste gas treatment system described in item 2 of the scope of patent application, wherein the cooler is further any one of a shell and tube cooler, a fin tube cooler or a plate heat exchanger cooler. 如申請專利範圍第1或2項所述之觸媒回流高效率有機廢氣處理系統，其中該淨氣排放管路的另一端係進一步連接一煙囪。 For the catalyst recirculation high-efficiency organic waste gas treatment system described in item 1 or 2 of the scope of patent application, the other end of the clean gas discharge pipeline is further connected with a chimney. 如申請專利範圍第1或2項所述之觸媒回流高效率有機廢氣處理系統，其中該冷卻氣輸送管路與該熱氣輸送管路之間係進一步設有一連通管路，該連通管路係設有一連通控制閥門，該熱氣輸送管路係設有一熱 氣控制閥門，並透過該連通控制閥門及該熱氣控制閥門來形成比例風門。 For example, the catalyst recirculation high-efficiency organic waste gas treatment system described in item 1 or 2 of the scope of patent application, wherein a communication pipeline is further provided between the cooling gas delivery pipeline and the hot gas delivery pipeline, and the communication pipeline Is equipped with a communication control valve, and the hot gas delivery pipeline is equipped with a heat A gas control valve, and a proportional air valve is formed through the communication control valve and the hot gas control valve. 如申請專利範圍第1或2項所述之觸媒回流高效率有機廢氣處理系統，其中該冷卻氣輸送管路與該熱氣輸送管路之間係進一步設有一聯通管路，該連通管路係設有一連通控制閥門，該冷卻氣輸送管路係設有一冷卻氣控制閥門，並透過該連通控制閥門及該冷卻氣控制閥門來形成比例風門。 For example, the catalyst recirculation high-efficiency organic waste gas treatment system described in item 1 or 2 of the scope of patent application, wherein a communication pipeline is further provided between the cooling gas delivery pipeline and the hot gas delivery pipeline, and the communication pipeline is A communication control valve is provided, and the cooling gas delivery pipeline is provided with a cooling gas control valve, and a proportional air valve is formed through the communication control valve and the cooling gas control valve. 如申請專利範圍第1或2項所述之觸媒回流高效率有機廢氣處理系統，其中該冷卻氣進氣管路係進一步輸送外氣至該吸附轉輪之冷卻區，且該外氣係為新鮮空氣。 For example, the catalyst recirculation high-efficiency organic waste gas treatment system described in item 1 or 2 of the scope of patent application, wherein the cooling air intake pipeline system further transports external air to the cooling zone of the adsorption runner, and the external air is fresh air. 如申請專利範圍第1或2項所述之觸媒回流高效率有機廢氣處理系統，其中該冷卻氣進氣管路係進一步設有一氣體旁通管路，該氣體旁通管路之一端係與該冷卻氣進氣管路連接，該氣體旁通管路之另一端係與該廢氣進氣管路連接。 For example, the catalyst recirculation high-efficiency organic waste gas treatment system described in item 1 or 2 of the scope of patent application, wherein the cooling gas inlet pipeline is further provided with a gas bypass pipeline, and one end of the gas bypass pipeline is connected with The cooling gas inlet pipeline is connected, and the other end of the gas bypass pipeline is connected with the exhaust gas inlet pipeline. 如申請專利範圍第1或2項所述之觸媒回流高效率有機廢氣處理系統，其中該淨氣排放管路係進一步設有一風車。 For example, the catalyst recirculation high-efficiency organic waste gas treatment system described in item 1 or 2 of the scope of patent application, wherein the clean gas discharge pipeline is further provided with a windmill. 一種觸媒回流高效率有機廢氣處理方法，主要係用於該有機廢氣處理系統，係包括有一觸媒床、一吸附反應床、一第一加熱器、一吸附轉輪、一第二加熱器、一第一熱交換器及一第二熱交換器，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，該第一熱交換器係設有第一冷側管路及第 一熱側管路，該第一熱交換器係連接有一第一熱氣回收管路、一第一觸媒床熱氣回收管路及一第一脫附濃縮氣體輸送管路，該第二熱交換器係設有第二冷側管路及第二熱側管路，該第二熱交換器係連接有一第二脫附濃縮氣體輸送管路及一第二熱氣回收管路，該第一加熱器係設有一第一加熱器輸送管路，該吸附反應床係設有一吸附反應床輸送管路，而該處理方法的主要步驟係包括：吸附區吸附：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進行吸附，再將吸附後之氣體透過該淨氣排放管路的另一端來進行輸送；冷卻區冷卻：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冷卻區之冷卻氣輸送到該第二加熱器內；脫附區脫附：透過與該第二加熱器的另一端所連接的熱氣輸送管路來將熱氣體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二熱交換器之第二冷側管路的一端；脫附濃縮氣體輸送：該脫附濃縮氣體再透過該第二熱交換器之第二冷側管路的另一端所連接的第二脫附濃縮氣體輸送管路來輸送到該第一熱交換器之第一冷側管路的一端，並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脫附濃縮氣體輸送管路來輸送到該第一加熱器內；吸附反應床吸附：將經由該第一加熱器進行加熱升溫的脫附濃縮氣體透 過該第一加熱器輸送管路來輸送至該吸附反應床來進行吸附；觸媒床處理：將經過該吸附反應床進行吸附的脫附濃縮氣體再透過該吸附反應床輸送管路來輸送到觸媒床內進行處理；觸媒床氣體輸送：將經過觸媒床處理後之氣體透過該觸媒床之出氣口所連接的第一觸媒床熱氣回收管路輸送到該第一熱交換器之第一熱側管路的一端，再由該第一熱交換器之第一熱側管路的另一端所連接的第一熱氣回收管路輸送到該第二熱交換器之第二熱側管路的一端；以及觸媒床氣體回收輸送：將輸送到該第二熱交換器之第二熱側管路的觸媒床之氣體，再經由與該第二熱交換器之第二熱側管路的另一端所連接的第二熱氣回收管路來輸送到該廢氣進氣管路連接。 A catalyst refluxing high-efficiency organic waste gas treatment method is mainly used in the organic waste gas treatment system. It includes a catalyst bed, an adsorption reaction bed, a first heater, an adsorption runner, a second heater, A first heat exchanger and a second heat exchanger. The adsorption runner system is provided with an adsorption zone, a cooling zone and a desorption zone. The adsorption runner system is connected with an exhaust gas inlet pipeline and a clean gas discharge pipeline , A cooling gas inlet pipeline, a cooling gas delivery pipeline, a hot gas delivery pipeline and a desorption concentrated gas pipeline, the first heat exchanger is provided with a first cold side pipeline and a second A hot side pipeline, the first heat exchanger is connected with a first hot gas recovery pipeline, a first catalyst bed hot gas recovery pipeline, and a first desorption concentrated gas delivery pipeline; the second heat exchanger A second cold side pipeline and a second hot side pipeline are provided. The second heat exchanger is connected to a second desorption concentrated gas delivery pipeline and a second hot gas recovery pipeline. The first heater is A first heater delivery pipeline is provided, and the adsorption reaction bed is provided with an adsorption reaction bed delivery pipeline. The main steps of the treatment method include: adsorption in the adsorption zone: passing exhaust gas through the other end of the exhaust gas inlet pipeline It is sent to one side of the adsorption zone of the adsorption runner for adsorption, and then the adsorbed gas is transported through the other end of the clean gas discharge pipeline; cooling zone cooling: through the other end of the cooling gas inlet pipeline One end is used to deliver cooling air to the cooling zone of the adsorption runner for cooling, and then the cooling air passing through the cooling zone is delivered to the second heater through the other end of the cooling air delivery pipeline; the desorption zone desorption: The hot gas is transported to the desorption zone of the adsorption rotor through the hot gas delivery pipeline connected to the other end of the second heater for desorption, and then the desorption is performed through the other end of the desorption concentrated gas pipeline. The attached concentrated gas is delivered to one end of the second cold side pipeline of the second heat exchanger; the desorbed enriched gas delivery: the desorbed concentrated gas passes through the other end of the second cold side pipeline of the second heat exchanger. The second desorption concentrated gas delivery pipeline is connected to one end of the first cold-side pipeline of the first heat exchanger, and then passes through the other end of the first cold-side pipeline of the first heat exchanger. The first desorption concentrated gas delivery pipeline is connected to the first heater; the adsorption reaction bed adsorption: the desorption concentrated gas heated by the first heater is permeated The first heater transfer pipeline is transported to the adsorption reaction bed for adsorption; catalyst bed treatment: the desorption concentrated gas that has passed through the adsorption reaction bed for adsorption is transported to the adsorption reaction bed transfer pipeline Treatment in the catalyst bed; catalyst bed gas transportation: the gas after the catalyst bed treatment is transported to the first heat exchanger through the first catalyst bed hot gas recovery pipeline connected to the outlet of the catalyst bed One end of the first hot side pipeline of the first heat exchanger is transported to the second hot side of the second heat exchanger by the first hot gas recovery pipeline connected to the other end of the first hot side pipeline of the first heat exchanger One end of the pipeline; and the catalyst bed gas recovery and transportation: the gas sent to the catalyst bed of the second hot side pipeline of the second heat exchanger, and then through the second hot side of the second heat exchanger The second hot gas recovery pipeline is connected to the other end of the pipeline to be connected to the exhaust gas inlet pipeline. 一種觸媒回流高效率有機廢氣處理方法，主要係用於該有機廢氣處理系統，係包括有一觸媒床、一吸附反應床、一第一加熱器、一吸附轉輪、一第二加熱器、一第二熱交換器及一冷卻器，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，該第二熱交換器係設有第二冷側管路及第二熱側管路，該第二熱交換器係連接有一第二脫附濃縮氣體輸送管路及一第二熱氣回收管路，該第一加熱器係設有一第一加熱器輸送管路，該吸附反應床係設有一吸附反應床輸送管路，該冷卻器係設有冷卻水管路，該冷卻器係連接有一冷卻熱氣回收管路及一觸媒床熱氣回收管路，而該處理方法的主要步驟係包括：吸附區吸附：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 吸附區的一側進行吸附，再將吸附後之氣體透過該淨氣排放管路的另一端來進行輸送；冷卻區冷卻：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冷卻區之冷卻氣輸送到該第二加熱器內；脫附區脫附：透過與該第二加熱器的另一端所連接的熱氣輸送管路來將熱氣體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二熱交換器之第二冷側管路的一端；脫附濃縮氣體輸送：該脫附濃縮氣體再透過該第二熱交換器之第二冷側管路的另一端所連接的第二脫附濃縮氣體輸送管路來輸送到該第一加熱器內；吸附反應床吸附：將經由該第一加熱器進行加熱升溫的脫附濃縮氣體透過該第一加熱器輸送管路來輸送至該吸附反應床來進行吸附；觸媒床處理：將經過該吸附反應床進行吸附的脫附濃縮氣體再透過該吸附反應床輸送管路來輸送到觸媒床內進行處理；觸媒床氣體輸送：將經過觸媒床處理後之氣體透過該觸媒床之出氣口所連接的觸媒床熱氣回收管路輸送到該冷卻器內，再由該冷卻器之另一端所連接的冷卻熱氣回收管路輸送到該第二熱交換器之第二熱側管路的一端；以及觸媒床氣體回收輸送：將輸送到該第二熱交換器之第二熱側管路的觸媒床之氣體，再經由與該第二熱交換器之第二熱側管路的另一端所連接的 第二熱氣回收管路來輸送到該廢氣進氣管路連接。 A catalyst refluxing high-efficiency organic waste gas treatment method is mainly used in the organic waste gas treatment system. It includes a catalyst bed, an adsorption reaction bed, a first heater, an adsorption runner, a second heater, A second heat exchanger and a cooler. The adsorption runner system is provided with an adsorption zone, a cooling zone and a desorption zone. The adsorption runner system is connected with an exhaust gas intake pipeline, a clean gas discharge pipeline, and a cooling zone. Air intake pipeline, a cooling gas delivery pipeline, a hot gas delivery pipeline and a desorption concentrated gas pipeline, the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, The second heat exchanger is connected with a second desorption concentrated gas delivery pipeline and a second hot gas recovery pipeline, the first heater is provided with a first heater delivery pipeline, and the adsorption reaction bed is provided with a Adsorption reaction bed transport pipeline, the cooler is provided with a cooling water pipeline, the cooler is connected with a cooling hot gas recovery pipeline and a catalyst bed hot gas recovery pipeline, and the main steps of the treatment method include: adsorption zone Adsorption: The exhaust gas is sent to the adsorption runner through the other end of the exhaust gas inlet pipe One side of the adsorption zone is adsorbed, and then the adsorbed gas is transported through the other end of the clean gas discharge pipeline; cooling zone cooling: Cooling gas is delivered to the adsorption through the other end of the cooling gas inlet pipeline The cooling zone of the runner is cooled, and then the cooling gas passing through the cooling zone is sent to the second heater through the other end of the cooling gas delivery pipeline; the desorption zone desorption: through the second heater The hot gas delivery pipeline connected to the other end transports the hot gas to the desorption zone of the adsorption rotor for desorption, and then transports the desorption concentrated gas to the second heat through the other end of the desorption concentrated gas pipeline. One end of the second cold side pipeline of the exchanger; desorption concentrated gas transport: the desorption concentrated gas passes through the second desorption concentrated gas connected to the other end of the second cold side pipeline of the second heat exchanger Transport pipeline to the first heater; adsorption reaction bed adsorption: the desorption concentrated gas heated by the first heater is sent to the adsorption reaction bed through the first heater delivery pipeline. Adsorption; catalyst bed treatment: the desorption concentrated gas that has been adsorbed by the adsorption reaction bed is transported to the catalyst bed for processing through the adsorption reaction bed transfer pipeline; catalyst bed gas transportation: will pass through the catalyst The gas after bed treatment is sent to the cooler through the catalyst bed hot gas recovery pipeline connected to the outlet of the catalyst bed, and then sent to the first cooling device by the cooling hot gas recovery pipeline connected to the other end of the cooler One end of the second hot-side pipeline of the second heat exchanger; and catalyst bed gas recovery and transportation: the gas sent to the catalyst bed of the second hot-side pipeline of the second heat exchanger is passed through and the first Second heat exchanger connected to the other end of the second hot side pipeline The second hot gas recovery pipeline is connected to the exhaust gas and the intake pipeline. 如申請專利範圍第14或15項所述之觸媒回流高效率有機廢氣處理方法，其中該第二熱交換器之第二熱氣回收管路係進一步設有一除塵設備，該除塵設備係為袋式除塵器、電袋式複合除塵器、慣性除塵器、靜電除塵器、離心式除塵器、濾筒式脈衝除塵器、脈衝袋式除塵器、脈衝濾芯除塵器、脈衝噴吹袋式除塵器、濕式除塵器、濕式電除塵器、濕式靜電除塵器、水膜除塵器、文丘里管除塵器、旋風分離器、煙道除塵器、多層除塵器、負壓反吹濾袋除塵器、低壓長袋脈衝除塵器、臥式靜電除塵器、無動力除塵器、荷電水霧除塵器、多管旋風除塵器、防爆除塵器之其中任一。 For example, the catalyst reflux high-efficiency organic waste gas treatment method described in item 14 or 15 of the scope of patent application, wherein the second hot gas recovery pipeline of the second heat exchanger is further provided with a dust removal device, which is a bag type Dust collector, electric bag composite dust collector, inertial dust collector, electrostatic precipitator, centrifugal dust collector, filter cartridge pulse dust collector, pulse bag filter, pulse filter dust collector, pulse jet bag filter, wet Type dust collector, wet electrostatic precipitator, wet electrostatic precipitator, water film dust collector, venturi tube dust collector, cyclone separator, flue dust collector, multi-layer dust collector, negative pressure back blow filter bag dust collector, low pressure Any one of long bag pulse dust collector, horizontal electrostatic dust collector, unpowered dust collector, charged water mist dust collector, multi-tube cyclone dust collector, explosion-proof dust collector. 如申請專利範圍第14或15項所述之觸媒回流高效率有機廢氣處理方法，其中該第二熱交換器之第二熱氣回收管路係進一步設有一濾網裝置，該濾網裝置係用於進行除塵使用。 For example, the catalyst recirculation high-efficiency organic waste gas treatment method described in the scope of patent application 14 or 15, wherein the second hot gas recovery pipeline of the second heat exchanger is further provided with a filter device, and the filter device is used Used for dust removal. 如申請專利範圍第14或15項所述之觸媒回流高效率有機廢氣處理方法，其中該第一加熱器及該第二加熱器係進一步分別為電加熱器，該電加熱器係採用電熱絲、電熱管或電熱片之其中任一種。 For example, the catalyst recirculation high-efficiency organic waste gas treatment method described in item 14 or 15 of the scope of patent application, wherein the first heater and the second heater are further respectively electric heaters, and the electric heater adopts electric heating wire , Either of electric heating tube or electric heating film. 如申請專利範圍第14或15項所述之觸媒回流高效率有機廢氣處理方法，其中該第一加熱器及該第二加熱器係進一步分別為管道加熱器，該管道加熱器係採用氣體燃料或液體燃料之其中任一種。 For example, the catalyst recirculation high-efficiency organic waste gas treatment method described in item 14 or 15 of the scope of patent application, wherein the first heater and the second heater are further pipeline heaters respectively, and the pipeline heater uses gas fuel Or any of the liquid fuels. 如申請專利範圍15項所述之觸媒回流高效率有機廢氣處理方法，其中該冷卻器係進一步為殼管式冷卻器、鰭管式冷卻器或板式熱交換器冷卻器之其中任一。 According to the catalytic reflux high-efficiency organic waste gas treatment method described in the scope of the patent application, the cooler is further any one of a shell and tube cooler, a fin tube cooler or a plate heat exchanger cooler. 如申請專利範圍第14或15項所述之觸媒回流高效率有機廢氣處理方法，其中該淨氣排放管路的另一端係進一步連接一煙囪。 As described in item 14 or 15 of the scope of patent application, the catalyst reflux high-efficiency organic waste gas treatment method, wherein the other end of the clean gas discharge pipeline is further connected with a chimney. 如申請專利範圍第14或15項所述之觸媒回流高效率有機廢氣處理方法，其中該冷卻氣輸送管路與該熱氣輸送管路之間係進一步設有一連通管路，該連通管路係設有一連通控制閥門，該熱氣輸送管路係設有一熱氣控制閥門，並透過該連通控制閥門及該熱氣控制閥門來形成比例風門。 For example, the catalyst reflux high-efficiency organic waste gas treatment method described in item 14 or 15 of the scope of patent application, wherein a communication pipeline is further provided between the cooling gas delivery pipeline and the hot gas delivery pipeline, and the communication pipeline A communication control valve is provided, and the hot gas delivery pipeline is provided with a hot gas control valve, and a proportional air valve is formed through the communication control valve and the hot gas control valve. 如申請專利範圍第14或15項所述之觸媒回流高效率有機廢氣處理方法，其中該冷卻氣輸送管路與該熱氣輸送管路之間係進一步設有一聯通管路，該連通管路係設有一連通控制閥門，該冷卻氣輸送管路係設有一冷卻氣控制閥門，並透過該連通控制閥門及該冷卻氣控制閥門來形成比例風門。 For example, the catalyst recirculation high-efficiency organic waste gas treatment method described in item 14 or 15 of the scope of patent application, wherein a communication pipeline is further provided between the cooling gas delivery pipeline and the hot gas delivery pipeline, and the communication pipeline is A communication control valve is provided, and the cooling gas delivery pipeline is provided with a cooling gas control valve, and a proportional air valve is formed through the communication control valve and the cooling gas control valve. 如申請專利範圍第14或15項所述之觸媒回流高效率有機廢氣處理方法，其中該冷卻氣進氣管路係進一步輸送外氣至該吸附轉輪之冷卻區，且該外氣係為新鮮空氣。 For example, the catalyst refluxing high-efficiency organic waste gas treatment method described in item 14 or 15 of the scope of patent application, wherein the cooling gas intake pipeline system further transports external air to the cooling zone of the adsorption runner, and the external air system is fresh air. 如申請專利範圍第14或15項所述之觸媒回流高效率有機廢氣處理方法，其中該冷卻氣進氣管路係進一步設有一氣體旁通管路，該氣體旁通管路之一端係與該冷卻氣進氣管路連接，該氣體旁通管路之另一端係與該廢氣進氣管路連接。 For example, the catalyst recirculation high-efficiency organic waste gas treatment method described in the scope of patent application 14 or 15, wherein the cooling gas intake pipeline is further provided with a gas bypass pipeline, and one end of the gas bypass pipeline is connected with The cooling gas inlet pipeline is connected, and the other end of the gas bypass pipeline is connected with the exhaust gas inlet pipeline. 如申請專利範圍第14或15項所述之觸媒回流高效率有機廢氣處理方法，其中該淨氣排放管路係進一步設有一風車。 For example, the catalyst recirculation high-efficiency organic waste gas treatment method described in item 14 or 15 of the scope of patent application, wherein the clean gas discharge pipeline is further provided with a windmill.
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