TW202246702A - Runner system with heat transfer oil and method thereof with which the incinerated gas can be processed through the hot side pipeline of the furnace heat exchanger, and circulated through the heat transfer oil system to improve processing efficiency - Google Patents
Runner system with heat transfer oil and method thereof with which the incinerated gas can be processed through the hot side pipeline of the furnace heat exchanger, and circulated through the heat transfer oil system to improve processing efficiency Download PDFInfo
- Publication number
- TW202246702A TW202246702A TW110119521A TW110119521A TW202246702A TW 202246702 A TW202246702 A TW 202246702A TW 110119521 A TW110119521 A TW 110119521A TW 110119521 A TW110119521 A TW 110119521A TW 202246702 A TW202246702 A TW 202246702A
- Authority
- TW
- Taiwan
- Prior art keywords
- pipeline
- heat exchanger
- cold
- medium oil
- heat medium
- Prior art date
Links
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
- F23G7/061—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
- F23G7/065—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/46—Recuperation of heat
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Lubrication Of Internal Combustion Engines (AREA)
Abstract
Description
本發明係有關於一種具熱媒油之轉輪系統及其方法，尤指一種具有提升有機廢氣處理效率，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 runner system with heat medium oil and its method, especially to an organic waste gas treatment system or similar equipment that can improve the efficiency of organic waste gas treatment and is suitable for semiconductor industry, photoelectric 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。 Press, at present, volatile organic gases (VOC) are produced in the manufacturing process of the semiconductor industry or the optoelectronic industry. Therefore, processing equipment for processing volatile organic gases (VOC) will be installed in each factory area to avoid (VOC) directly into the air and 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 emission.
但是近年來，政府對空氣汙染非常重視，也因此在煙囪的排放標準上訂定了有關大氣品質標準，同時將依國際管制趨勢發展，逐期檢討。 However, in recent years, the government has attached great importance to air pollution. Therefore, it has established relevant air quality standards for chimney emission standards. At the same time, it will be reviewed periodically in accordance with the development of international control trends.
因此，本發明人有鑑於上述缺失，期能提出一種具有提升有機廢氣處理效率的具熱媒油之轉輪系統及其方法，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 shortcomings, the inventor hopes to propose a rotary system with heat medium oil and its method that can improve the efficiency of organic waste gas treatment, so that users can easily operate and assemble. To provide user convenience, which is the motive of the invention that the inventor intends to develop.
本發明之主要目的，在於提供一種具熱媒油之轉輪系統及其 方法，主要係透過增加一熱媒油系統之設計，該熱媒油系統係設有一熱媒油槽、一進氣熱交換器及一爐膛熱交換器，該進氣熱交換器係設於該廢氣進氣管路上，該爐膛熱交換器係設於該直燃式焚燒爐(TO)之爐膛內，使來源廢氣能經過該進氣熱交換器之熱側管路進行加熱處理，而焚燒後之氣體能經過該爐膛熱交換器之熱側管路進行處理，並透過該熱媒油系統來回循環，以具有提升有機廢氣處理效率，進而增加整體之實用性。 The main purpose of the present invention is to provide a runner system with heat medium oil and its The method is mainly through the design of adding a heat medium oil system. The heat medium oil system is provided with a heat medium oil tank, an air intake heat exchanger and a furnace heat exchanger. The air intake heat exchanger is located in the waste gas On the intake pipeline, the furnace heat exchanger is installed in the furnace of the direct-fired incinerator (TO), so that the exhaust gas from the source can be heated through the hot side pipeline of the intake heat exchanger, and the incinerated The gas can be processed through the hot side pipeline of the furnace heat exchanger, and circulated back and forth through the heat medium oil system to improve the efficiency of organic waste gas treatment, thereby increasing the overall practicability.
本發明之另一目的，在於提供一種具熱媒油之轉輪系統及其方法，其中該熱媒油系統係設有一熱媒油槽、一進氣熱交換器及一爐膛熱交換器所組成該熱媒油系統之熱媒油槽係以熱媒為熱源，而該熱媒係呈液態之油品，該熱媒能經該進氣熱媒油輸出管路、該進氣熱媒油輸入管路、該爐膛熱媒油輸出管路及該爐膛熱媒油輸入管路來進行循環加熱使用，使能透過循環方式讓來源廢氣的相對溼度降低，以具有提升進入吸附轉輪之吸附區吸附之效能，進而增加整體之吸附性。 Another object of the present invention is to provide a runner system with heat medium oil and its method, wherein the heat medium oil system is composed of a heat medium oil tank, an air inlet heat exchanger and a furnace heat exchanger. The heat medium oil tank of the heat medium oil system uses the heat medium as the heat source, and the heat medium is liquid oil. The heat medium can pass through the intake heat medium oil output pipeline and the intake heat medium oil input pipeline. . The furnace heat medium oil output pipeline and the furnace heat medium oil input pipeline are used for circulating heating, so that the relative humidity of the source exhaust gas can be reduced through circulation, so as to improve the adsorption efficiency of the adsorption area entering the adsorption wheel , thereby increasing the overall adsorption.
本發明之次一目的，在於提供一種具熱媒油之轉輪系統及其方法，透過該吸附轉輪之脫附區需透過熱氣來進行，而該熱氣之來源有兩種，第一種為該直燃式焚燒爐(TO)內設有第三熱交換器，該第三熱交換器係設於該爐膛熱交換器與該第一熱交換器之間或是設於該第二熱交換器與該爐膛熱交換器之間，且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，而該熱氣輸送管路的另一端係與該第三熱交換器之第三冷側管路的另一端連接，另第二種為設有一加熱器，其中該加熱器係為空氣對空氣熱交換器、液體對空氣熱交換器、電加熱器、瓦斯加熱器之其中任一種，而該熱氣輸送管路的另一端係與該加熱器連接，且該熱氣輸送管路的 一端係與該吸附轉輪之脫附區的另一側連接，使該吸附轉輪之脫附區能具有高溫脫附之效果，進而增加整體之操作性。 The second object of the present invention is to provide a runner system with heat medium oil and its method. The desorption zone of the adsorption runner needs to be carried out through hot gas, and there are two sources of the hot gas. The first one is The direct-fired incinerator (TO) is provided with a third heat exchanger, the third heat exchanger is set between the furnace heat exchanger and the first heat exchanger or is set in the second heat exchanger Between the heat exchanger and the furnace heat exchanger, and one end of the hot gas delivery pipeline is connected to the other side of the desorption area of the adsorption wheel, and the other end of the hot gas delivery pipeline is connected to the third heat exchange The other end of the third cold side pipeline of the device is connected, and the second type is provided with a heater, wherein the heater is an air-to-air heat exchanger, a liquid-to-air heat exchanger, an electric heater, a gas heater any of them, and the other end of the hot gas delivery pipeline is connected to the heater, and the hot gas delivery pipeline One end is connected to the other side of the desorption area of the adsorption wheel, so that the desorption area of the adsorption wheel can have the effect of high temperature desorption, thereby increasing the overall operability.
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 related to the present invention, but the attached drawings are only for reference and illustration, and are not intended to limit the present invention.
10:直燃式焚燒爐(TO) 10: Direct fired incinerator (TO)
101:爐頭 101: Stove head
102:爐膛 102: Furnace
11:入口 11: Entrance
12:出口 12: Export
20:第一熱交換器 20: First heat exchanger
21:第一冷側管路 21: The first cold side pipeline
22:第一熱側管路 22: The first hot side pipeline
30:第二熱交換器 30: Second heat exchanger
31:第二冷側管路 31: Second cold side pipeline
32:第二熱側管路 32: Second hot side pipeline
40:第三熱交換器 40: The third heat exchanger
41:第三冷側管路 41: The third cold side pipeline
42:第三熱側管路 42: The third hot side pipeline
50:加熱器 50: heater
61:第一冷側輸送管路 61: The first cold side delivery pipeline
62:第二冷側輸送管路 62: Second cold side delivery pipeline
70:吸附轉輪 70: Adsorption runner
701:吸附區 701: adsorption area
702:冷卻區 702: cooling zone
703:脫附區 703: Desorption area
71:廢氣進氣管路 71: Exhaust gas intake pipe
711:廢氣連通管路 711: Exhaust gas communication pipeline
7111:廢氣連通控制閥門 7111: Exhaust gas connection control valve
712:風機 712: fan
72:淨氣排放管路 72: Net gas discharge pipeline
721:風機 721: fan
73:冷卻氣進氣管路 73: Cooling air intake pipe
74:冷卻氣輸送管路 74: Cooling air delivery pipeline
75:熱氣輸送管路 75: Hot gas delivery pipeline
76:脫附濃縮氣體管路 76: Desorption concentrated gas pipeline
761:風機 761: fan
80:煙囪 80: chimney
90:熱媒油系統 90: Heat medium oil system
91:熱媒油槽 91: heat medium oil tank
911:進氣熱媒油輸出管路 911: Intake heat medium oil output pipeline
912:進氣熱媒油輸入管路 912: Intake heat medium oil input pipeline
913:爐膛熱媒油輸出管路 913: Furnace heat medium oil output pipeline
914:爐膛熱媒油輸入管路 914: Furnace heat medium oil input pipeline
92:進氣熱交換器 92: Air intake heat exchanger
921:冷側管路 921: cold side piping
922:熱側管路 922: hot side piping
93:爐膛熱交換器 93: furnace heat exchanger
931:冷側管路 931: cold side pipeline
932:熱側管路 932: hot side piping
S100:來源廢氣進行輸送 S100: Source exhaust gas for transportation
S110:來源廢氣通過進氣熱交換器 S110: The source exhaust gas passes through the intake air heat exchanger
S120:吸附轉輪進行吸附 S120: Adsorption by the adsorption wheel
S130:輸入冷卻區冷卻氣 S130: Input the cooling air in the cooling zone
S140:脫附區進行脫附 S140: Desorption in the desorption area
S150:脫附濃縮氣體輸送 S150: Desorption concentrated gas delivery
S160:焚燒後之氣體進行輸送 S160: Transportation of incinerated gas
S170:焚燒後之氣體通過爐膛熱交換器 S170: The incinerated gas passes through the furnace heat exchanger
S180:焚燒後之氣體出口輸出 S180: Gas outlet output after incineration
S200:來源廢氣進行輸送 S200: Source exhaust gas for transportation
S210:來源廢氣通過進氣熱交換器 S210: The source exhaust gas passes through the intake heat exchanger
S220:吸附轉輪進行吸附 S220: Adsorption by the adsorption wheel
S230:輸入冷卻區冷卻氣 S230: Input the cooling air in the cooling zone
S240:脫附區進行脫附 S240: Desorption in the desorption area
S250:脫附濃縮氣體輸送 S250: Desorption Concentrated Gas Delivery
S260:焚燒後之氣體進行輸送 S260: Transportation of incinerated gas
S270:焚燒後之氣體通過爐膛熱交換器 S270: The gas after incineration passes through the furnace heat exchanger
S280:焚燒後之氣體出口輸出 S280: Gas outlet output after incineration
S300:來源廢氣進行輸送 S300: Source exhaust gas for conveying
S310:來源廢氣通過進氣熱交換器 S310: Source exhaust gas passes through the intake heat exchanger
S320:吸附轉輪進行吸附 S320: adsorption wheel for adsorption
S330:輸入冷卻區冷卻氣 S330: Input the cooling air in the cooling zone
S340:脫附區進行脫附 S340: Desorption in the desorption area
S350:脫附濃縮氣體輸送 S350: Desorption Concentrated Gas Delivery
S360:焚燒後之氣體進行輸送 S360: Transportation of incinerated gas
S370:焚燒後之氣體通過爐膛熱交換器 S370: The gas after incineration passes through the furnace heat exchanger
S380:焚燒後之氣體出口輸出 S380: Gas outlet output after incineration
第1圖係為本發明之主要實施態樣的系統架構示意圖。 Figure 1 is a schematic diagram of the system architecture of the main implementation of the present invention.
第2圖係為本發明之主要實施態樣具有風機的系統架構示意圖。 Fig. 2 is a schematic diagram of a system architecture with a fan in the main embodiment of the present invention.
第3圖係為本發明之主要實施態樣中第三熱交換器具不同位置的系統架構示意圖。 Fig. 3 is a schematic diagram of the system structure of different positions of the third heat exchange device in the main implementation mode of the present invention.
第4圖係為本發明之主要實施態樣中第三熱交換器具不同位置及風機的系統架構示意圖。 Fig. 4 is a schematic diagram of the system architecture of different positions and fans of the third heat exchange device in the main embodiment of the present invention.
第5圖係為本發明之另一實施態樣的系統架構示意圖。 FIG. 5 is a schematic diagram of the system architecture of another embodiment of the present invention.
第6圖係為本發明之另一實施態樣具有風機的系統架構示意圖。 Fig. 6 is a schematic diagram of a system architecture with a fan in another embodiment of the present invention.
第7圖係為本發明之主要實施態樣的步驟流程圖。 Fig. 7 is a flow chart of the steps of the main implementation of the present invention.
第8圖係為本發明之第二實施態樣的步驟流程圖。 Fig. 8 is a flow chart of the steps of the second embodiment of the present invention.
第9圖係為本發明之第三實施態樣的步驟流程圖。 Fig. 9 is a flow chart of the steps of the third embodiment of the present invention.
請參閱第1~9圖，係為本發明實施例之示意圖，而本發明之具熱媒油之轉輪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，以具有提升 有機廢氣處理效率。 Please refer to Figures 1 to 9, which are schematic diagrams of embodiments of the present invention, and the best implementation of the present invention's runner system with heat medium oil and its method is applied to the semiconductor industry, optoelectronic industry or chemical related industries Volatile organic waste gas treatment system or similar equipment to have improved Organic waste gas treatment efficiency.
而本發明具熱媒油之轉輪系統，主要係包括有一直燃式焚燒爐(TO)10、一第一熱交換器20、一第二熱交換器30、一第三熱交換器40、一第一冷側輸送管路61、一第二冷側輸送管路62、一吸附轉輪70、一煙囪80及一熱媒油系統90的組合設計(如第1圖至第2圖所示)，其中該第一熱交換器20係設有第一冷側管路21及第一熱側管路22，該第二熱交換器30係設有第二冷側管路31及第二熱側管路32，該第三熱交換器40係設有第三冷側管路41及第三熱側管路42。另該直燃式焚燒爐(TO)10係設有一爐頭101及一爐膛102，該爐頭101係與該爐膛102係相通，且該第一熱交換器20、第二熱交換器30及第三熱交換器40係分別設於該直燃式焚燒爐(TO)10之爐膛102內，而該直燃式焚燒爐(TO)10係設有入口11及出口12，且該入口11係設於該爐頭101處，而該直燃式焚燒爐(TO)10之出口12係連接至該煙囪80，藉此，使有機廢氣能由該入口11來進入該爐頭101內進行燃燒，再讓經過燃燒後之氣體能穿過該爐膛102，並由該出口11來排出至煙囪80處進行排放，以具有節省能源之效能。
And the runner system of the tool heat medium oil of the present invention mainly comprises a direct fired incinerator (TO) 10, a
另本發明之吸附轉輪70係設有吸附區701、冷卻區702及脫附區703，該吸附轉輪70係連接有一廢氣進氣管路71、一淨氣排放管路72、一冷卻氣進氣管路73、一冷卻氣輸送管路74、一熱氣輸送管路75及一脫附濃縮氣體管路76(如第1圖至第2圖所示)。其中該吸附轉輪70係為沸石濃縮轉輪或是其他材質之濃縮轉輪。而該廢氣進氣管路71的一端係連接至該吸附轉輪70之吸附區701的一側，
使該廢氣進氣管路71能將來源廢氣輸送到該吸附轉輪70之吸附區701的一側，而該淨氣排放管路72的一端係與該吸附轉輪70之吸附區701的另一側連接，該淨氣排放管路72的另一端來與該煙囪80連接，且該淨氣排放管路72係設有一風機721(如第2圖所示)，使能透過該風機721來將該淨氣排放管路72內的經過吸附後之氣體推拉到該煙囪80內以進行排放。
In addition, the
另該吸附轉輪70之冷卻區702的一側係連接該冷卻氣進氣管路73，以供氣體進入該吸附轉輪70之冷卻區702來進行冷卻使用，而該吸附轉輪70之冷卻區702的另一側係連接該冷卻氣輸送管路74的一端，該冷卻氣輸送管路74的另一端則與該第三熱交換器40之第三冷側管路41的一端連接(如第1圖至第2圖所示)，以將進入該吸附轉輪70之冷卻區702後之氣體輸送到該第三熱交換器40內進行熱交換。再者，該熱氣輸送管路75的一端係與該吸附轉輪70之脫附區703的另一側連接，且該熱氣輸送管路75的另一端係與該第三熱交換器40之第三冷側管路41的另一端連接，以能將經由該第三熱交換器40進行熱交換的高溫熱氣透過該熱氣輸送管路75來輸送到該吸附轉輪70之脫附區703來進行脫附使用。
In addition, one side of the
而上述該吸附轉輪70之冷卻區702係設有兩種實施方式，其中第一種實施方式為該吸附轉輪70之冷卻區702的一側所連接的冷卻氣進氣管路73乃是供新鮮空氣或外氣進入(如第1圖所示)，透過該新鮮空氣或外氣來提供該吸附轉輪70之冷卻區702降溫用。另第二種實施方式係該廢氣進氣管路71係設有一廢氣連通管路711，而該
廢氣連通管路711的另一端係與該冷卻氣進氣管路73連接(如第2圖所示)，以能透過該廢氣連通管路711來將該廢氣進氣管路71內的來源廢氣輸送到該吸附轉輪70之冷卻區702以進行降溫使用，另該廢氣連通管路711係設有一廢氣連通控制閥門7111(如第2圖所示)，以控制該廢氣連通管路711的風量。
The above-mentioned
另該脫附濃縮氣體管路76的一端係與該吸附轉輪70之脫附區703的一側連接，而該脫附濃縮氣體管路76的另一端係與該第一熱交換器20之第一冷側管路21的一端連接，其中該第一熱交換器20之第一冷側管路21的另一端係與該第一冷側輸送管路61的一端連接，該第一冷側輸送管路61的另一端則與該第二熱交換器30之第二冷側管路31的一端連接，而該第二熱交換器30之第二冷側管路31的另一端係與該第二冷側輸送管路62的一端連接，且該第二冷側輸送管路62的另一端則與該直燃式焚燒爐(TO)10之入口11連接(如第1圖至第2圖所示)，以能將經過高溫所脫附下來的脫附濃縮氣體能透過該脫附濃縮氣體管路76來輸送到該第一熱交換器20之第一冷側管路21的一端內，且由該第一熱交換器20之第一冷側管路21的另一端來輸送到該第一冷側輸送管路61的一端內，並由該第一冷側輸送管路61的另一端來輸送到該第二熱交換器30之第二冷側管路31的一端內，再由該第二熱交換器30之第二冷側管路31的另一端來輸送到該第二冷側輸送管路62的一端內，最後由該第二冷側輸送管路62的另一端來輸送到該直燃式焚燒爐(TO)10之入口11內，使能讓該直燃式焚燒爐(TO)10的爐頭101來進行高溫裂解，以能減少揮發性有機化合物。另該脫附濃縮氣體管路
76係設有一風機761(如第2圖所示)，以能將脫附濃縮氣體來推拉進入該第一熱交換器20之第一冷側管路21的一端內。
In addition, one end of the desorption concentrated
再者，本發明主要係透過增加一熱媒油系統90之設計，該熱媒油系統90係設有一熱媒油槽91、一進氣熱交換器92及一爐膛熱交換器93，且該熱媒油槽91係設有一進氣熱媒油輸出管路911、一進氣熱媒油輸入管路912、一爐膛熱媒油輸出管路913及一爐膛熱媒油輸入管路914(如第1圖至第2圖所示)，另該進氣熱交換器92係設於該廢氣進氣管路71上，該進氣熱交換器92係設有一冷側管路921及一熱側管路922，而該冷側管路921的一端係與該熱媒油槽91之進氣熱媒油輸出管路911連接，且該冷側管路921的另一端係與該熱媒油槽91之進氣熱媒油輸入管路912連接，該廢氣進氣管路71的來源廢氣先進入該進氣熱交換器92之熱側管路922的一端後，再由該進氣熱交換器92之熱側管路922的另一端輸出，並經由該廢氣進氣管路71來輸送至該吸附轉輪70之吸附區701的一側。另該廢氣進氣管路71係設有一風機712(如第2圖所示)，以能將來源廢氣來推拉進入該進氣熱交換器92之熱側管路922的一端內。
Furthermore, the present invention is mainly designed by increasing a heat
另外，該爐膛熱交換器93係設於該直燃式焚燒爐(TO)10之爐膛102內，該爐膛熱交換器93係設有一冷側管路931及一熱側管路932(如第1圖至第2圖所示)，而該冷側管路931的一端係與該熱媒油槽91之爐膛熱媒油輸出管路913連接，且該冷側管路931的另一端係與該熱媒油槽91之爐膛熱媒油輸入管路914連接，另該爐膛熱交換器93之熱側管路932的一端係與該第二熱交換器30之第二
熱側管路32的另一端連接(如第1圖至第2圖所示)，而該爐膛熱交換器93之熱側管路932的另一端係與該第三熱交換器40之第三熱側管路42的一端連接。
In addition, the
而上述之該熱媒油系統90之熱媒油槽91係以熱媒為熱源，而該熱媒係呈液態之油品，該熱媒能經該進氣熱媒油輸出管路911、該進氣熱媒油輸入管路912、該爐膛熱媒油輸出管路913及該爐膛熱媒油輸入管路914來進行循環加熱使用，使能透過循環方式讓來源廢氣的相對溼度降低，以具有提升進入該吸附轉輪70之吸附區701吸附之效能。
And the above-mentioned heat
而上述之直燃式焚燒爐(TO)10之爐頭101係能將經過焚燒後之氣體先輸送到該第二熱交換器30之第二熱側管路32的一側以進行熱交換，再由該第二熱交換器30之第二熱側管路32的另一側來將經過焚燒後之氣體再輸送到該爐膛熱交換器93之熱側管路932內(如第1圖至第2圖所示)，且焚燒後之氣體通過該爐膛熱交換器93之熱側管路932後，再輸送到該第三熱交換器40之第三熱側管路42的一側以進行熱交換，之後再由該第三熱交換器40之第三熱側管路42的另一側來將經過焚燒後之氣體再輸送到該第一熱交換器20之第一熱側管路22的一側以進行熱交換，最後由該第一熱交換器20之第一熱側管路22的另一側來輸送到該直燃式焚燒爐(TO)10之出口12，再由該直燃式焚燒爐(TO)10之出口12來輸送到煙囪80(如第1圖至第2圖所示)，以透過該煙囪80來進行排放。
The
另本發明的爐膛熱交換器93可以配合第三熱交換器40
需要溫度較高的焚燒後之氣體來調整在該直燃式焚燒爐(TO)10之爐膛102內的位置，該直燃式焚燒爐(TO)10之爐頭101係能將經過焚燒後之氣體先輸送到該第二熱交換器30之第二熱側管路32的一側以進行熱交換，再由該第二熱交換器30之第二熱側管路32的另一側來將經過焚燒後之氣體再輸送到該第三熱交換器40之第三熱側管路42內(如第3圖至第4圖所示)且焚燒後之氣體通過該第三熱交換器40之第三熱側管路42後，再輸送到該爐膛熱交換器93之熱側管路932的一側以進行熱交換，之後再由該爐膛熱交換器93之熱側管路932的另一側來將經過焚燒後之氣體再輸送到該第一熱交換器20之第一熱側管路22的一側以進行熱交換，最後由該第一熱交換器20之第一熱側管路22的另一側來輸送到該直燃式焚燒爐(TO)10之出口12，再由該直燃式焚燒爐(TO)10之出口12來輸送到煙囪80(如第3圖至第4圖所示)，以透過該煙囪80來進行排放。
In addition, the
再者，本發明具熱媒油之轉輪系統的另一實施態樣(如第5圖至第6圖所示)，其中該中的直燃式焚燒爐(TO)10、第一熱交換器20、第二熱交換器30、第一冷側輸送管路61、第二冷側輸送管路62、吸附轉輪70、煙囪80及熱媒油系統90是採與上述相同之設計，因此，上述的直燃式焚燒爐(TO)10、第一熱交換器20、第二熱交換器30、第一冷側輸送管路61、第二冷側輸送管路62、吸附轉輪70、煙囪80及熱媒油系統90內容不在重複，請參考上述之說明內容。
Furthermore, another embodiment of the runner system with heat medium oil of the present invention (as shown in Fig. 5 to Fig. 6), wherein the direct-fired incinerator (TO) 10, the first heat exchange The
而上述之差異乃為在於另一實施態樣中將原來該熱氣輸送管路75的另一端所連接設於該直燃式焚燒爐(TO)10之爐膛102內的
第三熱交換器40拿掉，並讓該熱氣輸送管路75的另一端改連接一個另外設在該直燃式焚燒爐(TO)10之爐膛102外的加熱器50(如第5圖至第6圖所示)，其中該加熱器50係為空氣對空氣熱交換器、液體對空氣熱交換器、電加熱器、瓦斯加熱器之其中任一種，使該吸附轉輪70之冷卻區702的另一側所連接的冷卻氣輸送管路74的另一端係與該加熱器50連接(如第5圖至第6圖所示)，以將進入該吸附轉輪70之冷卻區702後之氣體輸送到該加熱器50內進行加熱，而該熱氣輸送管路75的一端係與該吸附轉輪70之脫附區703的另一側連接，且該熱氣輸送管路75的另一端係與該加熱器50連接，以能將經由該加熱器50加熱後的高溫熱氣透過該熱氣輸送管路75來輸送到該吸附轉輪70之脫附區703來進行脫附使用。
The above-mentioned difference is that in another embodiment, the other end of the original hot
而本發明具熱媒油之轉輪方法，主要係包括有一直燃式焚燒爐(TO)10、一第一熱交換器20、一第二熱交換器30、一第三熱交換器40、一第一冷側輸送管路61、一第二冷側輸送管路62、一吸附轉輪70、一煙囪80及一熱媒油系統90的組合設計(如第1圖至第2圖所示)，其中該第一熱交換器20係設有第一冷側管路21及第一熱側管路22，該第二熱交換器30係設有第二冷側管路31及第二熱側管路32，該第三熱交換器40係設有第三冷側管路41及第三熱側管路42，該第一冷側輸送管路61的一端係與該第一冷側管路21的另一端連接，該第一冷側輸送管路61的另一端係與該第二冷側管路31的一端連接，該第二冷側輸送管路62的一端係與該第二冷側管路31的另一端連接，該第二冷側輸送管路62的另一端係與該直燃式焚燒爐(TO)10之入口1
1連接。另該直燃式焚燒爐(TO)10係設有一爐頭101及一爐膛102，該爐頭101係與該爐膛102係相通，且該第一熱交換器20、第二熱交換器30及第三熱交換器40係分別設於該直燃式焚燒爐(TO)之爐膛102內(如第1圖至第2圖所示)，而該直燃式焚燒爐(TO)10係設有入口11及出口12，且該入口11係設於該爐頭101處，且該直燃式焚燒爐(TO)10之出口12係連接至該煙囪80，另該熱媒油系統90係設有一熱媒油槽91、一進氣熱交換器92及一爐膛熱交換器93，該熱媒油槽91係設有一進氣熱媒油輸出管路911、一進氣熱媒油輸入管路912、一爐膛熱媒油輸出管路913及一爐膛熱媒油輸入管路914(如第1圖至第2圖所示)，藉此，使該有機廢氣能由該入口11來進入該爐頭101內進行燃燒，再讓經過燃燒後之氣體能穿過該爐膛102並由該出口12來排出至煙囪80處進行排放，以具有節省能源之效能。
And the runner method of tool heat medium oil of the present invention mainly comprises a direct fired incinerator (TO) 10, a
另本發明之吸附轉輪70係設有吸附區701、冷卻區702及脫附區703，該吸附轉輪70係連接有一廢氣進氣管路71、一淨氣排放管路72、一冷卻氣進氣管路73、一冷卻氣輸送管路74、一熱氣輸送管路75及一脫附濃縮氣體管路76(如第1圖至第2圖所示)。其中該吸附轉輪70係為沸石濃縮轉輪或是其他材質之濃縮轉輪。
In addition, the
其中該熱媒油系統90之熱媒油槽係以熱媒為熱源，而該熱媒係呈液態之油品，該熱媒能經該進氣熱媒油輸出管路911、該進氣熱媒油輸入管路912、該爐膛熱媒油輸出管路913及該爐膛熱媒油輸入管路914來進行循環加熱使用，使能透過循環方式讓來源廢氣的相對溼度降低，以具有提升進入吸附轉輪70之吸附區701吸附之效能。另該
進氣熱交換器92係設於該廢氣進氣管路71上，該進氣熱交換器92係設有一冷側管路921及一熱側管路922(如第1圖至第2圖所示)，該冷側管路921的一端係與該熱媒油槽91之進氣熱媒油輸出管路911連接，該冷側管路921的另一端係與該熱媒油槽91之進氣熱媒油輸入管路912連接。再者，該爐膛熱交換器93係設於該直燃式焚燒爐(TO)10之爐膛102內，該爐膛熱交換器93係設有一冷側管路931及一熱側管路932(如第1圖至第2圖所示)，該冷側管路931的一端係與該熱媒油槽91之爐膛熱媒油輸出管路913連接，該冷側管路931的另一端係與該熱媒油槽91之爐膛熱媒油輸入管路914連接。
Wherein the heat medium oil tank of the heat
而該主要實施態樣的方法步驟(如第7圖所示)係包括：步驟S100來源廢氣進行輸送：將來源廢氣透過該廢氣進氣管路71輸送到該進氣熱交換器92之熱側管路922的一端。而完成上述步驟S100後即進行下一步驟S110。
The method steps (as shown in FIG. 7 ) of the main implementation mode include: step S100 source exhaust gas is transported: the source exhaust gas is transported to the hot side of the
另，下一步進行的步驟S110來源廢氣通過進氣熱交換器：該來源廢氣通過該進氣熱交換器92之熱側管路922後，再由該進氣熱交換器92之熱側管路922的另一端輸出，且透過該廢氣進氣管路71來輸送至該吸附轉輪70之吸附區701的一側。而完成上述步驟S110後即進行下一步驟S120。
In addition, in the next step S110, the source exhaust gas passes through the intake heat exchanger: after the source exhaust gas passes through the
其中上述之步驟S100及步驟S110中該廢氣進氣管路的來源廢氣先進入該進氣熱交換器92之熱側管路922的一端後，再由該進氣熱交換器92之熱側管路922的另一端輸出，並經由該廢氣進氣管路來輸送至該吸附轉輪之吸附區的一側。另該廢氣進氣管路71係設
有一風機712(如第2圖所示)，以能將來源廢氣來推拉進入該進氣熱交換器92之熱側管路922的一端內。
Wherein the source exhaust gas of the exhaust gas intake pipeline in the above step S100 and step S110 first enters one end of the
另，下一步進行的步驟S120吸附轉輪進行吸附：透過該吸附轉輪70之吸附區701進行吸附後，由該吸附轉輪70之吸附區701的另一側將吸附後之氣體透過該淨氣排放管路72的另一端來輸出。而完成上述步驟S120後即進行下一步驟S130。
In addition, the step S120 carried out in the next step is adsorption by the adsorption wheel: after the adsorption is carried out through the
其中上述之步驟S120中該淨氣排放管路72的一端係與該吸附轉輪70之吸附區701的另一側連接，該淨氣排放管路72的另一端來與該煙囪80連接(如第1圖至第2圖所示)，且該淨氣排放管路72係設有一風機721(如第2圖所示)，使能透過該風機721來將該淨氣排放管路72內的經過吸附後之氣體推拉到該煙囪80內以進行排放。
Wherein in the above-mentioned step S120, one end of the clean
另，下一步進行的步驟S130輸入冷卻區冷卻氣：透過該冷卻氣進氣管路73的另一端來輸送冷卻氣至該吸附轉輪70之冷卻區702進行冷卻，再透過該冷卻氣輸送管路74的另一端來將經過該吸附轉輪70之冷卻區702的冷卻氣輸送到該第三熱交換器40之第三冷側管路41的一端。而完成上述步驟S130後即進行下一步驟S140。
In addition, in the next step S130, the cooling air is input into the cooling zone: through the other end of the cooling
其中上述之步驟S130中該吸附轉輪70之冷卻區702的一側係連接該冷卻氣進氣管路73，以供氣體進入該吸附轉輪70之冷卻區702來進行冷卻使用，而該吸附轉輪70之冷卻區702的另一側係連接該冷卻氣輸送管路74的一端(如第1圖至第2圖所示)，該冷卻氣輸送管路74的另一端則與該第三熱交換器40之第三冷側管路41
的一端連接，以將進入該吸附轉輪70之冷卻區702後之氣體輸送到該第三熱交換器40內進行熱交換。
Wherein the side of the
而上述吸附轉輪70之冷卻區702係設有兩種實施方式，其中第一種實施方式為該吸附轉輪70之冷卻區702的一側所連接的冷卻氣進氣管路73乃是供新鮮空氣或外氣進入(如第1圖所示)，透過該新鮮空氣或外氣來提供該吸附轉輪70之冷卻區702降溫用。另第二種實施方式係該廢氣進氣管路71係設有一廢氣連通管路711(如第2圖所示)，而該廢氣連通管路711的另一端係與該冷卻氣進氣管路73連接，以能透過該廢氣連通管路711來將該廢氣進氣管路71內的來源廢氣輸送到該吸附轉輪70之冷卻區702以進行降溫使用，另該廢氣連通管路711係設有一廢氣連通控制閥門7111(如第2圖所示)，以控制該廢氣連通管路711的風量。
And the
另，下一步進行的步驟S140脫附區進行脫附：透過與第三熱交換器40之第三冷側管路41的另一端所連接的熱氣輸送管路75來將熱氣輸送到該吸附轉輪70之脫附區703進行脫附，再透過該脫附濃縮氣體管路76的另一端來將脫附濃縮氣體輸送到該第一熱交換器20之第一冷側管路21的一端。而完成上述步驟S140後即進行下一步驟S150。
In addition, in the next step S140, the desorption area performs desorption: through the hot
其中上述之步驟S140中該熱氣輸送管路75的一端係與該吸附轉輪70之脫附區703的另一側連接，且該熱氣輸送管路75的另一端係與該第三熱交換器40之第三冷側管路41的另一端連接(如第1圖至第2圖所示)，以能將經由該第三熱交換器40進行熱交換的高
溫熱氣透過該熱氣輸送管路75來輸送到該吸附轉輪70之脫附區703來進行脫附使用。
One end of the hot
另，下一步進行的步驟S150脫附濃縮氣體輸送：該脫附濃縮氣體再透過該第一熱交換器20之第一冷側管路21的另一端所連接的第一冷側輸送管路61來輸送到該第二熱交換器30之第二冷側管路31的一端，且再透過該第二熱交換器30之第二冷側管路31的另一端所連接的第二冷側輸送管路62來輸送到該直燃式焚燒爐(TO)10之入口11。而完成上述步驟S150後即進行下一步驟S160。
In addition, the next step S150 is to transport the desorbed concentrated gas: the desorbed concentrated gas passes through the first cold
其中上述之步驟S150中第一熱交換器20之第一冷側管路21的另一端係與該第一冷側輸送管路61的一端連接，該第一冷側輸送管路61的另一端則與該第二熱交換器30之第二冷側管路31的一端連接，而該第二熱交換器30之第二冷側管路31的另一端係與該第二冷側輸送管路62的一端連接，且該第二冷側輸送管路62的另一端則與該直燃式焚燒爐(TO)10之入口11連接(如第1圖至第2圖所示)，以能將經過高溫所脫附下來的脫附濃縮氣體能透過該脫附濃縮氣體管路76來輸送到該第一熱交換器20之第一冷側管路21的一端內，且由該第一熱交換器20之第一冷側管路21的另一端來輸送到該第一冷側輸送管路61的一端內，並由該第一冷側輸送管路61的另一端來輸送到該第二熱交換器30之第二冷側管路31的一端內，再由該第二熱交換器30之第二冷側管路31的另一端來輸送到該第二冷側輸送管路62的一端內，最後由該第二冷側輸送管路62的另一端來輸送到該直燃式焚燒爐(TO)10之入口11內，使能讓該直燃式焚燒爐(TO)10的爐頭101來進行高溫裂
解，以能減少揮發性有機化合物。另該脫附濃縮氣體管路76係設有一風機761(如第2圖所示)，以能將脫附濃縮氣體來推拉進入該第一熱交換器20之第一冷側管路21的一端內。
The other end of the first cold-
另，下一步進行的步驟S160焚燒後之氣體進行輸送：將該直燃式焚燒爐(TO)10之爐頭101所燃燒後而產生的焚燒後之氣體輸送到該第二熱交換器30之第二熱側管路32的一端，且由該第二熱交換器30之第二熱側管路32的另一端輸送到該爐膛熱交換器93之熱側管路932的一端。而完成上述步驟S160後即進行下一步驟S170。
In addition, in the next step S160, the incinerated gas is transported: the incinerated gas produced by burning the
另，下一步進行的步驟S170焚燒後之氣體通過爐膛熱交換器：該焚燒後之氣體通過該爐膛熱交換器93之熱側管路932後，由該爐膛熱交換器93之熱側管路932的另一端輸出至該第三熱交換器40之第三熱側管路42的一端。而完成上述步驟S170後即進行下一步驟S180。
In addition, in the next step S170, the incinerated gas passes through the furnace heat exchanger: after the incinerated gas passes through the
另，下一步進行的步驟S180焚燒後之氣體出口輸出：該焚燒後之氣體再由該第三熱交換器40之第三熱側管路42的另一端輸送到該第一熱交換器20之第一熱側管路22的一端，最後由該第一熱交換器20之第一熱側管路22的另一端輸送到該直燃式焚燒爐(TO)10之出口12。
In addition, the output of the incinerated gas outlet in the next step S180: the incinerated gas is transported to the
其中該直燃式焚燒爐(TO)10之爐頭101係能將經過焚燒後之氣體先輸送到該第二熱交換器30之第二熱側管路32的一側以進行熱交換(如第1圖至第2圖所示)，再由該第二熱交換器30之第二熱側管路32的另一側來將經過焚燒後之氣體再輸送到該爐膛熱交換器93
之熱側管路932內，且焚燒後之氣體通過該爐膛熱交換器93之熱側管路932後，再輸送到該第三熱交換器40之第三熱側管路42的一側以進行熱交換，之後再由該第三熱交換器40之第三熱側管路42的另一側來將經過焚燒後之氣體再輸送到該第一熱交換器20之第一熱側管路22的一側以進行熱交換，最後由該第一熱交換器20之第一熱側管路22的另一側來輸送到該直燃式焚燒爐(TO)10之出口12，再由該直燃式焚燒爐(TO)10之出口12來輸送到煙囪80(如第1圖至第2圖所示)，以透過該煙囪80來進行排放。
Wherein the
另，本發明具熱媒油之轉輪方法中主要實施態樣(如第7圖所示)的步驟S100來源廢氣進行輸送、步驟S110來源廢氣通過進氣熱交換器、步驟S120吸附轉輪進行吸附、步驟S130輸入冷卻區冷卻氣、步驟S140脫附區進行脫附、步驟S150脫附濃縮氣體輸送、步驟S160焚燒後之氣體進行輸送、步驟S170焚燒後之氣體通過爐膛熱交換器及步驟S180焚燒後之氣體出口輸出，已於上述提出說明，請參考上述之說明內容。 In addition, in the runner method with heat medium oil of the present invention, the main implementation aspect (as shown in Figure 7) is that step S100 source exhaust gas is transported, step S110 source exhaust gas is passed through the intake heat exchanger, and step S120 is adsorbed by the runner. Adsorption, step S130 input cooling gas in the cooling zone, step S140 desorption in the desorption zone, step S150 desorption concentrated gas delivery, step S160 incineration gas delivery, step S170 incineration gas passing through the furnace heat exchanger and step S180 The gas outlet output after incineration has been explained above, please refer to the above explanation.
另本發明的爐膛熱交換器93可以配合第三熱交換器40需要溫度較高的焚燒後之氣體來調整在該直燃式焚燒爐(TO)10之爐膛102內的位置，而本發明的具有第三熱交換器40的第二實施態樣(如第8圖所示)中的步驟S200來源廢氣進行輸送、步驟S210來源廢氣通過進氣熱交換器、步驟S220吸附轉輪進行吸附、步驟S230輸入冷卻區冷卻氣、步驟S240脫附區進行脫附及步驟S250脫附濃縮氣體輸送都是採用與主要實施態樣(如第7圖所示)中的步驟S100來源
廢氣進行輸送、步驟S110來源廢氣通過進氣熱交換器、步驟S120吸附轉輪進行吸附、步驟S130輸入冷卻區冷卻氣、步驟S140脫附區進行脫附及步驟S150脫附濃縮氣體輸送之相同的設計，僅差異在於步驟S160焚燒後之氣體進行輸送、步驟S170焚燒後之氣體通過爐膛熱交換器及步驟S180焚燒後之氣體出口輸出之內容。
In addition, the
而具有第三熱交換器40的第二實施態樣之差異乃為步驟S260焚燒後之氣體進行輸送：將該直燃式焚燒爐(TO)10之爐頭101所燃燒後而產生的焚燒後之氣體輸送到該第二熱交換器30之第二熱側管路32的一端，且由該第二熱交換器30之第二熱側管路32的另一端輸送到該第三熱交換器40之第三熱側管路42的一端。而完成上述步驟S260後即進行下一步驟S270。
The difference of the second embodiment with the
另，下一步進行的步驟S270焚燒後之氣體通過爐膛熱交換器：該焚燒後之氣體由該第三熱交換器40之第三熱側管路42的另一端輸送到該爐膛熱交換器93之熱側管路932的一端，該焚燒後之氣體通過該爐膛熱交換器93之熱側管路932後，再由該爐膛熱交換器93之熱側管路932的另一端輸出。而完成上述步驟S270後即進行下一步驟S280。
In addition, in the next step S270, the incinerated gas passes through the furnace heat exchanger: the incinerated gas is transported to the
另，下一步進行的步驟S280焚燒後之氣體出口輸出：該焚燒後之氣體再由該爐膛熱交換器93之熱側管路932的另一端輸送到該第一熱交換器20之第一熱側管路22的一端，最後由該第一熱交換器20之第一熱側管路22的另一端輸送到該直燃式焚燒爐(TO)10之出口12。
In addition, the output of the incinerated gas outlet in step S280 carried out in the next step: the incinerated gas is transported to the first heat of the
其中該直燃式焚燒爐(TO)10之爐頭101係能將經過焚燒後之氣體先輸送到該第二熱交換器30之第二熱側管路32的一側以進行熱交換，再由該第二熱交換器30之第二熱側管路32的另一側來將經過焚燒後之氣體再輸送到該第三熱交換器40之第三熱側管路42內(如第3圖至第4圖所示)且焚燒後之氣體通過該第三熱交換器40之第三熱側管路42後，再輸送到該爐膛熱交換器93之熱側管路932的一側以進行熱交換，之後再由該爐膛熱交換器93之熱側管路932的另一側來將經過焚燒後之氣體再輸送到該第一熱交換器20之第一熱側管路22的一側以進行熱交換，最後由該第一熱交換器20之第一熱側管路22的另一側來輸送到該直燃式焚燒爐(TO)10之出口12，再由該直燃式焚燒爐(TO)10之出口12來輸送到煙囪80(如第3圖至第4圖所示)，以透過該煙囪80來進行排放。
Wherein the
再者，本發明具熱媒油之轉輪方法中主要實施態樣(如第7圖所示)的步驟S100來源廢氣進行輸送、步驟S110來源廢氣通過進氣熱交換器、S120吸附轉輪進行吸附、步驟S130輸入冷卻區冷卻氣、步驟S140脫附區進行脫附、步驟S150脫附濃縮氣體輸送、步驟S160焚燒後之氣體進行輸送、步驟S170焚燒後之氣體通過爐膛熱交換器及步驟S180焚燒後之氣體出口輸出，已於上述提出說明，請參考上述之說明內容。 Furthermore, in the runner method with heat medium oil of the present invention, the main implementation aspect (as shown in Figure 7) is that step S100 source exhaust gas is transported, step S110 source exhaust gas is carried out through the intake heat exchanger, and S120 adsorption runner Adsorption, step S130 input cooling gas in the cooling zone, step S140 desorption in the desorption zone, step S150 desorption concentrated gas delivery, step S160 incineration gas delivery, step S170 incineration gas passing through the furnace heat exchanger and step S180 The gas outlet output after incineration has been explained above, please refer to the above explanation.
而第三實施態樣(如第9圖所示)中的步驟S300來源廢氣進行輸送、步驟S310來源廢氣通過進氣熱交換器、S320吸附轉輪進行吸附、步驟S350脫附濃縮氣體輸送及步驟S360焚燒後之氣 體進行輸送都是採用與主要實施態樣(如第7圖所示)中的步驟S100來源廢氣進行輸送、步驟S110來源廢氣通過進氣熱交換器、S120吸附轉輪進行吸附、步驟S150脫附濃縮氣體輸送及步驟S160焚燒後之氣體進行輸送之相同的設計，僅差異在於步驟S130輸入冷卻區冷卻氣、步驟S140脫附區進行脫附、步驟S170焚燒後之氣體通過爐膛熱交換器及步驟S180焚燒後之氣體出口輸出之內容。 In the third embodiment (as shown in Figure 9), step S300 source exhaust gas is transported, step S310 source exhaust gas is adsorbed through the intake heat exchanger, S320 adsorption runner is adsorbed, step S350 desorption concentrated gas is transported, and steps S360 Gas after incineration The body is transported using the source exhaust gas in step S100 in the main implementation mode (as shown in Figure 7), the source exhaust gas in step S110 is adsorbed through the intake heat exchanger, S120 is adsorbed by the adsorption wheel, and desorbed in step S150 Condensed gas delivery and step S160 are the same design for delivery of incinerated gas, the only difference is that step S130 enters cooling gas in the cooling zone, step S140 desorption zone performs desorption, and step S170 the incinerated gas passes through the furnace heat exchanger and step S170. S180 Contents of gas outlet output after incineration.
因此，上述與步驟S300來源廢氣進行輸送、步驟S310來源廢氣通過進氣熱交換器、S320吸附轉輪進行吸附、步驟S350脫附濃縮氣體輸送及步驟S360焚燒後之氣體進行輸送之相同的內容不在重複，請參考上述之說明內容。下列將針對第三實施態樣(如第9圖所示)中的步驟S330輸入冷卻區冷卻氣、步驟S340脫附區進行脫附、步驟S370焚燒後之氣體通過爐膛熱交換器及步驟S380焚燒後之氣體出口輸出來進行說明。 Therefore, the same contents as those of step S300 for transporting the source exhaust gas, step S310 for the source exhaust gas to pass through the intake heat exchanger, S320 for adsorption by the adsorption runner, step S350 for transporting the desorbed concentrated gas, and step S360 for transporting the incinerated gas are not included. Repeat, please refer to the above description. The following will be aimed at the step S330 in the third embodiment (as shown in Figure 9) to input the cooling gas in the cooling zone, the desorption zone in the step S340 for desorption, the gas after the incineration in the step S370 is incinerated through the furnace heat exchanger and the step S380 The following gas outlet output is used for illustration.
而第三實施態樣之差異乃為步驟S330輸入冷卻區冷卻氣：透過該冷卻氣進氣管路73的另一端來輸送冷卻氣至該吸附轉輪70之冷卻區702進行冷卻，再透過該冷卻氣輸送管路74的另一端來將經過該吸附轉輪70之冷卻區702的冷卻氣輸出。而完成上述步驟S330後即進行下一步驟S340。
The difference of the third embodiment is that the cooling air in the cooling zone is input in step S330: through the other end of the cooling
另，下一步進行的步驟S340脫附區進行脫附：該熱氣輸送管路75之一端係與該吸附轉輪70之脫附區703連接，並由該吸附轉輪70之脫附區703進行脫附，再透過該脫附濃縮氣體管路76來將脫附濃縮氣體輸送到該第一熱交換器20之第一冷側管路21的一端。
In addition, the step S340 carried out in the next step is desorbed in the desorption area: one end of the hot
其中上述之步驟S330及步驟S340中熱氣輸送管路75係將原來另一端所連接設於該直燃式焚燒爐(TO)10之爐膛102內的第三熱交換器40拿掉，並讓該熱氣輸送管路75的另一端改連接一個另外設在該直燃式焚燒爐(TO)10之爐膛102外的加熱器50(如第5圖至第6圖所示)，其中該加熱器50係為空氣對空氣熱交換器、液體對空氣熱交換器、電加熱器、瓦斯加熱器之其中任一種，使該吸附轉輪70之冷卻區702的另一側所連接的冷卻氣輸送管路74的另一端係與該加熱器50連接，以將進入該吸附轉輪70之冷卻區702後之氣體輸送到該加熱器50內進加熱(如第5圖至第6圖所示)，而該熱氣輸送管路75的一端係與該吸附轉輪70之脫附區703的另一側連接，且該熱氣輸送管路75的另一端係與該加熱器50連接，以能將經由該加熱器50進行加熱的高溫熱氣透過該熱氣輸送管路75來輸送到該吸附轉輪70之脫附區來703進行脫附使用。 Wherein the above-mentioned step S330 and step S340 in the hot gas conveying pipeline 75 system, the third heat exchanger 40 that the original other end is connected and is located in the hearth 102 of this direct-fired incinerator (TO) 10 is removed, and let the The other end of the hot gas delivery pipeline 75 is connected to a heater 50 (as shown in Fig. 5 to Fig. 6 ) which is additionally located outside the hearth 102 of the direct-fired incinerator (TO) 10, wherein the heater 50 It is any one of air-to-air heat exchanger, liquid-to-air heat exchanger, electric heater, and gas heater, so that the cooling gas delivery pipeline connected to the other side of the cooling zone 702 of the adsorption runner 70 The other end of 74 is connected with the heater 50, so that the gas that enters the cooling zone 702 of the adsorption wheel 70 is transported to the heater 50 for heating (as shown in Figures 5 to 6), and One end of the hot gas delivery pipeline 75 is connected with the other side of the desorption zone 703 of the adsorption wheel 70, and the other end of the hot gas delivery pipeline 75 is connected with the heater 50, so that The high-temperature hot gas heated by the device 50 is transported to the desorption area of the adsorption wheel 70 through the hot gas delivery pipeline 75 to be desorbed 703 for use.
再者，步驟S370焚燒後之氣體通過爐膛熱交換器：該焚燒後之氣體通過該爐膛熱交換器93之熱側管路932後，由該爐膛熱交換器93之熱側管路932的另一端輸出至該第一熱交換器20之第一熱側管路22的一端。而完成上述步驟S370後即進行下一步驟S380。
Furthermore, the incinerated gas in step S370 passes through the furnace heat exchanger: after the incinerated gas passes through the
另，下一步進行的步驟S380焚燒後之氣體出口輸出：該焚燒後之氣體最後由該第一熱交換器20之第一熱側管路22的另一端輸送到該直燃式焚燒爐(TO)10之出口12。
In addition, the output of the gas outlet after the incineration of the step S380 carried out in the next step: the gas after the incineration is finally transported to the direct-fired incinerator (TO )10
其中上述之步驟S370及步驟S380中該直燃式焚燒爐(TO)10之爐頭101係能將經過焚燒後之氣體先輸送到該第二熱交換
器30之第二熱側管路32的一側以進行熱交換，再由該第二熱交換器30之第二熱側管路32的另一側來將經過焚燒後之氣體再輸送到該爐膛熱交換器93內，且焚燒後之氣體通過該爐膛熱交換器93後，再輸送到該第一熱交換器20之第一熱側管路22的一側以進行熱交換(如第5圖至第6圖所示)，最後由該第一熱交換器20之第一熱側管路22的另一側來輸送到該直燃式焚燒爐(TO)10之出口12，再由該直燃式焚燒爐(TO)10之出口12來輸送到煙囪80，以透過該煙囪80來進行排放。
Wherein the
由以上詳細說明，可使熟知本項技藝者明瞭本發明的確可達成前述目的，實已符合專利法之規定，爰提出發明專利申請。 From the above detailed description, those who are familiar with this art can understand that the present invention can indeed achieve the aforementioned purpose, and have actually met the provisions of the Patent Law, so they should file 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。 But the above-mentioned ones are only preferred embodiments of the present invention, and should not limit the scope of the present invention; therefore, all simple equivalent changes and modifications made according to the patent scope of the present invention and the contents of the description of the invention , should still fall within the scope covered by the patent of the present invention.
10:直燃式焚燒爐(TO) 10: Direct fired incinerator (TO)
101:爐頭 101: Stove head
102:爐膛 102: Furnace
11:入口 11: Entrance
12:出口 12: Export
20:第一熱交換器 20: First heat exchanger
21:第一冷側管路 21: The first cold side pipeline
22:第一熱側管路 22: The first hot side pipeline
30:第二熱交換器 30: Second heat exchanger
31:第二冷側管路 31: Second cold side pipeline
32:第二熱側管路 32: Second hot side pipeline
40:第三熱交換器 40: The third heat exchanger
41:第三冷側管路 41: The third cold side pipeline
42:第三熱側管路 42: The third hot side pipeline
61:第一冷側輸送管路 61: The first cold side delivery pipeline
62:第二冷側輸送管路 62: Second cold side delivery pipeline
70:吸附轉輪 70: Adsorption Wheel
701:吸附區 701: adsorption area
702:冷卻區 702: cooling zone
703:脫附區 703: Desorption area
71:廢氣進氣管路 71: Exhaust gas intake pipe
72:淨氣排放管路 72: Net gas discharge pipeline
73:冷卻氣進氣管路 73: Cooling air intake pipe
74:冷卻氣輸送管路 74: Cooling air delivery pipeline
75:熱氣輸送管路 75: Hot gas delivery pipeline
76:脫附濃縮氣體管路 76: Desorption concentrated gas pipeline
80:煙囪 80: chimney
90:熱媒油系統 90: Heat medium oil system
91:熱媒油槽 91: heat medium oil tank
911:進氣熱媒油輸出管路 911: Intake heat medium oil output pipeline
912:進氣熱媒油輸入管路 912: Intake heat medium oil input pipeline
913:爐膛熱媒油輸出管路 913: Furnace heat medium oil output pipeline
914:爐膛熱媒油輸入管路 914: Furnace heat medium oil input pipeline
92:進氣熱交換器 92: Air intake heat exchanger
921:冷側管路 921: cold side piping
922:熱側管路 922: hot side piping
93:爐膛熱交換器 93: furnace heat exchanger
931:冷側管路 931: cold side pipeline
932:熱側管路 932: hot side piping
Claims (22)
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| TW110119521A TWI811690B (en) | 2021-05-28 | 2021-05-28 | Rotor system with heat medium oil and method thereof |
| CN202110900419.2A CN115405937A (en) | 2021-05-28 | 2021-08-06 | Rotary wheel system with hot medium oil and method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| TW110119521A TWI811690B (en) | 2021-05-28 | 2021-05-28 | Rotor system with heat medium oil and method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| TW202246702A true TW202246702A (en) | 2022-12-01 |
| TWI811690B TWI811690B (en) | 2023-08-11 |
Family
ID=84156714
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| TW110119521A TWI811690B (en) | 2021-05-28 | 2021-05-28 | Rotor system with heat medium oil and method thereof |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN115405937A (en) |
| TW (1) | TWI811690B (en) |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5707229A (en) * | 1993-07-12 | 1998-01-13 | Durr Industries, Inc. | Regenerative thermal oxidizer with heat exchanger columns |
| JP4669863B2 (en) * | 2007-07-20 | 2011-04-13 | 株式会社日立製作所 | Gas treatment system containing volatile organic compounds |
| JP2009052845A (en) * | 2007-08-28 | 2009-03-12 | Sakae Murata | Exhaust gas treatment apparatus and boiler system |
| TW201617125A (en) * | 2014-11-06 | 2016-05-16 | Jg Environmental Tech Co Ltd | Organic exhaust adsorption concentration purification system and method thereof |
| CN205517129U (en) * | 2016-02-01 | 2016-08-31 | 杰智环境科技股份有限公司 | Use concentrated purification treatment system of waste gas of incinerator heat recovery |
| CN205730789U (en) * | 2016-05-13 | 2016-11-30 | 昆山工统环保科技有限公司 | Organic waste gas treatment system |
| CN106731483A (en) * | 2017-03-21 | 2017-05-31 | 上海兰宝环保科技有限公司 | It is suitable for the exhaust treatment system of high humility organic exhaust gas |
| TWM583922U (en) * | 2019-06-21 | 2019-09-21 | 華懋科技股份有限公司 | High-efficiency organic exhaust gas processing system with energy recovery function |
| TWM620908U (en) * | 2021-05-28 | 2021-12-11 | 華懋科技股份有限公司 | Rotor system with thermal medium oil |
-
2021
- 2021-05-28 TW TW110119521A patent/TWI811690B/en active
- 2021-08-06 CN CN202110900419.2A patent/CN115405937A/en active Pending
Also Published As
| Publication number | Publication date |
|---|---|
| CN115405937A (en) | 2022-11-29 |
| TWI811690B (en) | 2023-08-11 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| TWM604865U (en) | Energy-saving dual-wheel cold side pass temperature control system | |
| TWI756748B (en) | Energy-saving dual-rotor cold side bypass temperature control system and method thereof | |
| TWM620908U (en) | Rotor system with thermal medium oil | |
| TWI826737B (en) | Energy-saving single-runner hot side pass temperature control system and method thereof | |
| TWI823017B (en) | Energy-saving dual-runner high-concentration cold-side bypass temperature control system and method thereof | |
| TW202246702A (en) | Runner system with heat transfer oil and method thereof with which the incinerated gas can be processed through the hot side pipeline of the furnace heat exchanger, and circulated through the heat transfer oil system to improve processing efficiency | |
| CN214147937U (en) | Energy-saving single-runner high-concentration hot-side bypass over-temperature control system | |
| TW202015790A (en) | Rotor system with high temperature desorption and method thereof can remove the remaining Volatile Organic Compounds (VOC) to restore the adsorption capacity of the adsorption rotor | |
| TWM620880U (en) | Rotation wheel system having heat source | |
| CN214345424U (en) | Energy-saving double-rotating-wheel high-concentration hot-side bypass over-temperature control system | |
| TWI773310B (en) | Runner system with heat source and method therefor | |
| TWM608059U (en) | Energy-saving single-wheel hot side bypass over temperature control system | |
| TWI788715B (en) | Energy-saving dual-rotor high-concentration hot side bypass temperature control system and method | |
| TWM604867U (en) | Energy-saving dual-wheel high-concentration cold side pass temperature control system | |
| TWM606289U (en) | Energy-saving type hot side bypass temperature control system with dual runners | |
| TWI745007B (en) | Energy-saving single runner cold side passing temperature control system and method | |
| TWI826736B (en) | Energy-saving single-runner high-concentration hot side pass temperature control system and method thereof | |
| TWI738444B (en) | Energy-saving single-rotor high-concentration cold side passing temperature control system and method | |
| TWI823027B (en) | Energy-saving dual-runner hot side pass temperature control system and method thereof | |
| TWI826752B (en) | Double-runner high-concentration organic waste gas treatment system and method thereof | |
| CN214370247U (en) | Energy-saving single-runner high-concentration cold-side bypass over-temperature control system | |
| TWM604864U (en) | Energy-saving single-wheel cold side pass temperature control system | |
| TW202223298A (en) | Dual-runner high-efficiency organic waste gas treatment system and method thereof capable of improving the efficiency of organic waste gas treatment and providing the effect of energy saving and emission reduction | |
| TWM604866U (en) | Volatile organic waste gas treatment system with dual wheels | |
| TWM609440U (en) | Energy saving type single runner high concentration thermal bypass temperature control system |