M404366 五、新型說明： 【新型所屬之技術領域】 本創作係關於一種二段分離潔淨式廢熱氣回收裝置，特別 是指一種可達成空氣熱效率最高後排出之廢熱氣回收裝置。 【先前技術】 請參閱第一圖所示，為習用一段式廢熱氣回收裝置之整體 結構示意圖；其中該廢熱氣回收裝置丨係安裝並連結於數烘箱 11上，该烘箱11則將廢熱氣傳送至廢熱氣回收裝置！中，並 透過設置於廢熱器别欠裝置i内之熱交換器將廢氣冷卻後，再 傳送至排驗自I2 ’並透蝴氣煙自12將廢氣翻，藉以達 到廢熱氣回收之效。 堉芩閲第二圖所示，為 •「入/¾(:烈礼又农1之細部 結構示意圖；其包含有一烘箱u ’該烘箱u内設有一熱交換 益13 ’係可將進入烘箱n内之氣體溫度提高，並透過風扇μ 將增溫後之氣體加以利用，使用後之熱氣祕透過廢氣排出管 ㈣出至廢氣處理箱體16中，進入廢氣處理箱體Μ中之廢 就則透過其内之空氣_⑹加㈣滤，過毅之廢氣再透過 廢氣處理·㈣讀交換㈣將贿溫絲低，並傳送至 主排風管以__ 18將_出；廢氣處理箱體 16中之熱父換€ 13則與廢氣回收箱體19相互連接，並 氣回收箱體19之一滅·^古in ^ 、各 鮮扇191，透過送風風扇將新 鮮工氣傳私廢賴_以，顧由__將新⑸ 3 M404366 交換器13提㊉其溫度，於習用之裝置 度之新鮮空氣加熱至9(M2〇度後，再 至火、箱11中，藉此達到將廢氣回收 廢是’習用熱交換器13較高之溫度係由於吸收 &所排出之廢氣並將熱能吸收 13之溫度嶋M404366 V. New description: [New technical field] This creation is about a two-stage separation clean waste heat recovery device, especially a waste heat recovery device that can achieve the highest air heat efficiency after discharge. [Prior Art] Please refer to the first figure, which is a schematic diagram of the overall structure of a conventional one-stage waste heat recovery device; wherein the waste heat recovery device is installed and connected to the number of ovens 11, and the oven 11 transfers the waste heat gas. To waste heat recovery unit! The exhaust gas is cooled by the heat exchanger disposed in the waste heat device i, and then sent to the inspection and exhausted from the I2' and the exhaust gas is turned over from the exhaust gas to obtain the waste heat recovery. As shown in the second figure, it is “into/3⁄4 (: the structure of the details of the ritual and the agricultural 1; it contains an oven u 'the oven u has a heat exchange benefit 13 ' can enter the oven n The temperature of the gas inside is increased, and the heated gas is used by the fan μ. After use, the hot gas is passed through the exhaust gas discharge pipe (4) to the exhaust gas treatment tank 16, and the waste entering the exhaust gas treatment tank is passed through The air inside _(6) plus (4) filter, the exhaust gas of Yiyi and then the exhaust gas treatment. (4) Read exchange (4) The bribe is low and sent to the main exhaust pipe to __ 18 _ out; in the exhaust gas treatment tank 16 The hot father exchanges for 13 and is connected to the exhaust gas recovery tank 19, and one of the gas recovery tanks 19 is extinguished, and the fresh fan 191 is used to pass the fresh air to the private fan. The new (5) 3 M404366 exchanger 13 is raised by __, and the fresh air heated by the conventional device is heated to 9 (M2 〇 degree, then to the fire, the tank 11 to achieve the waste gas recycling waste is ' The higher temperature of the conventional heat exchanger 13 is due to absorption & exhaust gas and absorption of heat energy 13 Nakajima temperature
然而’上述抑廢熱氣回收装置雖可達到使用者之目的， 較差’故回收後之熱氣含有污染物，例如油 污、S02、N02、来立鹿望从》；w· 質，除造成廢氣回收效率不佳之外， 更=内物質受到回收廢氣之污染。況且，習見裝置只能 回收m或是翔回錄態熱能，無法共用細收裝置。 由此可見，上述習用廢熱氣回收裝置仍有諸多缺失，實非 -良善之設計I，而秘加以改良。However, the above-mentioned waste heat recovery unit can achieve the purpose of the user, which is poor. Therefore, the recovered hot gas contains pollutants, such as oil, S02, N02, and Luli Luwang, and the quality of exhaust gas is eliminated. In addition to the poor, the internal materials are contaminated by the recovered exhaust gas. Moreover, the device can only recover m or the back-recorded thermal energy, and cannot share the fine-receiving device. It can be seen that there are still many shortcomings in the above-mentioned conventional waste heat recovery device, which is not a good design I, but the secret is improved.
鮮空氣過遽後再透過熱 中’係將溫度為30-40 透過廢氣導入管193導 再利用之效果。 本案創作人鑑於上述制廢熱氣时裝置所衍生的各項 缺點，乃μ細改良_，並經多年苦心職潛心研究後， 終於成功研發完成本件廢熱氣回收裝置。 【新型内容】 本創作之目的係透過吸熱回收箱及放熱回收箱而可將廢 氣回收再糊’ _可達成线熱鱗最高後翻之廢熱氣回 收裝置。 為了達到上述目的，本創作係包含有吸翻收箱及放熱回[ 4 M404366 收粕並共用熱回收裝置之二相式（氣態及液態)共用熱回收裝 置；以下分別敘述： 本創作之吸熱时箱包含有—熱交換器，該触換器内係 設有位於熱交換翻之回收液態管，該回收液態管係分別設有 液悲入口及液態出口；熱交換器之一端則連接設有廢氣排出 管’該廢氣排出管則分別與至少—個以上之供箱相互連接；熱 交換益之另侧連接設有—風扇，該風細與織_相互連 接。 於操作使用時’該吸熱回收箱係透過廢氣排出管接收各烘 箱内之廢減，並透過熱交換H内之回收液態管之冷液將廢熱 氣降溫’降溫後之氣體則再利用風扇透過排氣煙自排出，此 時’因廢熱氣而增溫之回收液態管之熱液則可流入放熱回收箱 之熱交換器中。 本創作之放熱回收箱係包含有一熱交換器，該熱交換器内 亦設有回收液態管，該回收液態管係分別設有與吸熱回收箱之 回收液態管相互連接之液態入口及液態出口，該熱交換器之一 端係設有風車，熱交換器之另端則連接有一氣體導入管，該氣 體導入管則分別與至少一個以上之烘箱相互連接。 當新鮮空氣透過風車導入熱交換器中時，新鮮空氣則透過 來自吸熱回收箱之熱液，並透過回收液態管將新鮮空氣增溫， 增溫後之氣體則再透過氣體導入管導入各烘箱内，藉此達到廢 熱回收之效，更可避免廢熱回收後之氣體中含有雜質；冷卻後[ 5 之回收液態管内之液體則可再回流至吸熱回收箱之熱交換器 中，並再次透過吸熱回收箱之作動方式循環作動降溫，達到廢 熱回收運用之目的。 於一實施例中，該放熱回收箱之新鮮空氣係可自攝氏 30〜40度加熱至攝氏9〇〜120度之溫度。 【實施方式】 為讓本創作之上述和其他目的、特徵和優點能更明顯易 十重’下文特舉出較佳實施例，並配合所附圖式，作詳細說明如 下。 明參閱第二A圖所示，為本創作二段分離潔淨式廢熱氣 回收裝置之吸熱回收箱結構示意圖；該吸熱回收箱2包含有一 熱交換器2卜該熱交換器21内係設有位於熱交換器21内之 回收液態管2U ’該回收液態管211係分別設有液態入口 212 及液態出π 213 ;熱交換器21之—端則連接設有廢氣排出管 22，該廢氣排出管22則分別與至少一個以上之洪箱23相互連 接，熱交換器21之另端則連接設有一風| 24，該風扇24則 與排氣煙自25相互連接；該吸熱2魏過廢氣排出管 22接收各㈣23内之廢減，並透過熱錢H 21内之回收 液態管211之冷液將廢熱氣降溫’降溫後之氣體則再利用風扇 24透過排氣_25排出，此時，因廢熱氣㈣溫之回收液態 官211 主之熱賴可流人下狀放熱回收箱3之熱交換器对； 請參閲第三B圖所示’為本創作二段分離潔淨式廢熱氣⑸ M404366 回收裝置之放熱回收箱結構示意圖；該放熱回收箱3亦包含有 一熱父換器31 ,該熱交換器31内亦設有回收液態管311，該 回收液態管311係分別設有與吸熱回收箱2之回收液態管21 相互連接之液態入口 312及液態出口 313，該熱交換器31之 一鳊係设有風車32，熱交換器31之另端則連接有一氣體導入 管33，該氣體導入管33則分別與至少一個以上之烘箱34相 互連接； 當新鮮空氣透過風車32導入熱交換器31中時，新鮮空氣 則透過來自吸熱回收箱2之熱液，並透過回收液態管311將新 鮮空氣增溫，於本實施例中，該新鮮空氣係可自攝氏30〜40 度加熱至攝氏90〜120度之溫度，增溫後之氣體則再透過氣體 導入管33導入各烘箱34内，藉此達到廢熱回收之效，更可避 免廢熱回收後之氣體中含有雜質；冷卻後之回收液態管311内 之液體則可再回流至吸熱回收箱2之熱交換器21中，並再次 透過吸熱回收箱2之作動方式猶環作動降溫，達到廢熱回收運 用之目的。 本創作二段分離潔淨式廢熱氣回收裝置，實為一種創新的 二相式(氣態及液態)共用熱回收裝置，改善了習見只能回收氣 態熱此*或疋單獨回收液態熱能的缺失。 上列詳細說明係針對本創作之一可行實施例之具體說 明，惟該實施例並非用以限制本創作之專利範圍，凡未脫離本 創作技藝精神所為之等效實施或變更，均應包含於本案之專利f S] 7 範圍中。本創作之權梅護制應如後述之申請專利範圍所 【圖式簡單說明】 第1為制—段式廢熱氣回收裝置之㈣結構示意圖 意圖 第二圖為制-段式廢熱氣回收裝置之細部結構示" A圖為本_廢減畔数之吸細_結構示音圖 B圖林難廢減畔妓之 二 【主要元件符號制】 不思圖 第 ’、 第 1廢熱氣回收裝置 11烘箱 12排氣煙囪 13熱交換器 14風扇 15廢氣排出管 16廢氣處理箱體 161空氣濾網 17主排風管 18排氣風車 19廢氣回收箱體 191送風扇 192空氣濾網 193廢氣導入管 M404366 2吸熱回收箱 21熱交換器 211回收液態管 212液態入口 213液態出口 22廢氣排出管 23烘箱 24風扇 25排氣煙囪 3放熱回收箱 31熱交換器 311回收液態管 312液態入口 313液態出口 32風車 33氣體導入管 34烘箱After the fresh air has passed through the heat, the temperature is 30-40 and the effect is transmitted through the exhaust gas introduction pipe 193. In view of the above shortcomings caused by the above-mentioned equipment for the production of waste heat, the creators of this case have improved the _, and after years of painstaking research, finally successfully developed and completed the waste heat recovery device. [New content] The purpose of this creation is to recycle the waste gas through the heat recovery bin and the heat recovery bin. _ The waste heat recovery device with the highest heat scale can be reached. In order to achieve the above objectives, this creation consists of a two-phase (gaseous and liquid) shared heat recovery unit with a suction and return tank [4 M404366 and a heat recovery unit; the following are respectively described: The box comprises a heat exchanger, wherein the exchanger is provided with a recovery liquid pipe located in the heat exchange, wherein the recovered liquid pipe system is respectively provided with a liquid sad inlet and a liquid outlet; and one end of the heat exchanger is connected with exhaust gas. The exhaust pipe is connected to at least one or more of the supply tanks respectively; the other side of the heat exchange is connected with a fan, and the air is connected to the weave. During operation, the heat absorption recovery tank receives the waste reduction in each of the ovens through the exhaust gas discharge pipe, and cools the waste heat gas through the cold liquid of the recovered liquid pipe in the heat exchange H. The gas after the temperature is cooled is reused by the fan. The gas is self-discharged, and at this time, the hot liquid of the recovered liquid pipe which is heated by the waste heat gas can flow into the heat exchanger of the heat recovery recovery tank. The exothermic recovery tank of the present invention comprises a heat exchanger, and the heat exchanger is also provided with a recovery liquid pipe, which is respectively provided with a liquid inlet and a liquid outlet which are connected with the recovery liquid pipe of the heat absorption recovery tank. One end of the heat exchanger is provided with a windmill, and the other end of the heat exchanger is connected with a gas introduction pipe, and the gas introduction pipe is respectively connected to at least one of the ovens. When fresh air is introduced into the heat exchanger through the windmill, the fresh air passes through the hot liquid from the heat absorption recovery tank, and the fresh air is warmed through the recovery liquid pipe, and the heated gas is then introduced into each of the ovens through the gas introduction pipe. In order to achieve the effect of waste heat recovery, it is possible to avoid impurities in the gas after the waste heat recovery; after cooling, the liquid in the recovered liquid pipe can be returned to the heat exchanger of the heat absorption recovery tank and recovered again through the heat absorption. The operation mode of the box is cyclically actuated to cool down, and the purpose of waste heat recovery and utilization is achieved. In one embodiment, the fresh air of the exothermic recovery tank can be heated from 30 to 40 degrees Celsius to a temperature of 9 to 120 degrees Celsius. The above and other objects, features and advantages of the present invention will become more apparent and obvious. Referring to FIG. 2A, a schematic diagram of the structure of the heat absorption recovery tank of the second-stage separation clean waste heat recovery device is provided; the heat absorption recovery box 2 includes a heat exchanger 2, which is located in the heat exchanger 21 The recovered liquid pipe 2U in the heat exchanger 21 is provided with a liquid inlet 212 and a liquid outlet π 213 respectively; the end of the heat exchanger 21 is connected with an exhaust gas discharge pipe 22, and the exhaust gas discharge pipe 22 is connected. Each of the heat exchangers 21 is connected to at least one of the flood boxes 23, and the other end of the heat exchanger 21 is connected to a wind | 24, and the fan 24 is connected to the exhaust fumes 25; the heat absorption 2 passes through the exhaust gas exhaust pipe 22 Receiving the waste reduction in each (4) 23, and cooling the waste heat gas through the cold liquid of the recovered liquid pipe 211 in the hot money H 21 'the temperature is cooled, and then the gas is discharged through the exhaust gas _25 by the fan 24, at this time, due to the waste heat gas (4) The heat recovery of the liquid official 211 is the heat exchanger of the heat-reducing heat-recovery box 3; please refer to the third section of Figure 2 for the creation of the second-stage separation clean waste heat gas (5) M404366 recovery unit Schematic diagram of the heat recovery recovery tank; The heat recovery tank 3 also includes a hot parent converter 31. The heat exchanger 31 is also provided with a recovery liquid pipe 311, which is respectively provided with a liquid liquid connected to the recovered liquid pipe 21 of the heat absorption recovery tank 2. The inlet 312 and the liquid outlet 313, one of the heat exchangers 31 is provided with a windmill 32, and the other end of the heat exchanger 31 is connected with a gas introduction pipe 33, and the gas introduction pipe 33 is respectively connected to at least one of the ovens 34. When the fresh air is introduced into the heat exchanger 31 through the windmill 32, the fresh air passes through the hot liquid from the heat absorption recovery tank 2, and the fresh air is warmed through the recovery liquid tube 311. In this embodiment, the fresh air is fresh. The air system can be heated from 30 to 40 degrees Celsius to a temperature of 90 to 120 degrees Celsius, and the heated gas is introduced into each of the ovens 34 through the gas introduction pipe 33, thereby achieving the effect of waste heat recovery and avoiding waste heat recovery. The gas in the latter contains impurities; the liquid in the recovered liquid pipe 311 after cooling can be returned to the heat exchanger 21 of the heat absorption recovery tank 2, and again through the operation of the heat absorption recovery tank 2 , To achieve the object transported by the waste heat recovery. The second-stage separation clean waste heat recovery unit of this creation is an innovative two-phase (gaseous and liquid) shared heat recovery device, which improves the lack of recovery of gaseous heat from the recovery of gaseous heat. The detailed description above is a detailed description of one of the possible embodiments of the present invention, and the embodiment is not intended to limit the scope of the patents, and the equivalent implementations or modifications that are not included in the spirit of the present invention should be included in The patent in this case is in the range of f S] 7. The right to protect the creation of this creation should be as described in the patent application scope [Simplified description of the drawings] The first is the system-section waste heat recovery unit (four) structure schematic intention The second picture is the system-stage waste heat recovery unit Detailed structure shows " A picture is _ waste reduction number of the number of suction _ structure sound map B Tulin difficult to reduce the side of the second [main component symbol system] not thinking of the first, the first waste heat recovery device 11 oven 12 exhaust chimney 13 heat exchanger 14 fan 15 exhaust gas discharge pipe 16 exhaust gas treatment tank 161 air filter 17 main exhaust pipe 18 exhaust windmill 19 exhaust gas recovery tank 191 send fan 192 air filter 193 exhaust gas introduction pipe M404366 2 endothermic recovery tank 21 heat exchanger 211 recovery liquid tube 212 liquid inlet 213 liquid outlet 22 exhaust gas discharge pipe 23 oven 24 fan 25 exhaust chimney 3 heat recovery bin 31 heat exchanger 311 recovery liquid pipe 312 liquid inlet 313 liquid outlet 32 Windmill 33 gas introduction pipe 34 oven