M407096 淨化成效不穩定。 再按，熱泵之工作原理，係以壓縮機不斷地抽吸和壓 縮冷煤，使冷媒在封閉系統中掂援 ㈣衣相變’而把環境之熱能 藉蒸發器加以吸收，並由冷凝器將冷水加熱成熱水；其所 消耗之能量為壓縮機維持冷媒循環所耗費之電能，故根據 能量不變定律：冷凝器輸出之熱能=輸入壓縮機之電能+ 蒸發器自環境吸收之熱能。 又按廢an巾通常會存在錢網所無法濾除之微 粒’而此等微粒乃會堵塞住活性碳或彿石等吸附材之孔 洞，，降低吸附材之吸附能力，且—旦微粒堵塞於吸附材之 孔洞後就難以去除，吸㈣之使料命遂因此縮短。 【新型内容】 本創作之主要目的，係欲解決先前技術易受到天候影 響而淨化成效不穩定H而具有淨化成效穩定不受天 候影響之功效。 本創作之另一目的，則具有節能之功效。 本創作之又一目的，乃具有延長吸附材使用壽命之功效。 為達上述功效，本創作之結構特徵，係將製程所產生 含有有機溶劑之待淨化廢氣導人—吸脫附裝置，並於該吸 脫附裝置之下游端設置-淨化裝置，另於該吸脫附裝置之 上游端設置一用以升溫之熱交換器者。 此外，進一步設置一熱泵連結該熱交換器，讓該熱交 換器與該熱泵之冷凝器進行熱交換。又，進一步於該熱交 換器之上游端没置一洗蘇器。另，進一步令該洗蘇器與該 熱果連結’讓洗務水與該熱系之蒸發器進行熱交換而冷卻。 再者，該熱交換器藉由該熱泵穩定調節其升溫程度，而 該熱泵乃根據待淨化廢氣之溫度與相對濕度（或露點溫度）調 節該熱父換器之升溫程度。然而，該熱交換器致使導入該吸 脫附裝置之待淨化廢氣之相對濕度維持在60%RH以下。另 一，該吸脫附裝置為流體化式濃縮器或固定床式濃縮器。又 一，該淨化裝置為焚化爐、冷凝器、喷霧室或喷霧加臭氧室。 再一，該吸脫附裝置之吸附材為活性碳或沸石。 【實施方式】 首先，請參閱第三圖所示，本創作之第一實施例，係 將製程所產生含有有機溶劑之待淨化廢氣導入一吸脫附裝 置（10)，俾以對待淨化廢氣中之有機溶劑進行吸附與濃縮 脫附之程序，而該吸脫附裝置（10)可為流體化式濃縮器或 固定床式濃縮器；再於該吸脫附裝置（10)之下游端設置一 淨化裝置（20)，進而對藉由該吸脫附裝置（1〇)濃縮脫附出 來之有機溶劑，進行焚化爐焚化或冷凝器回收之淨化處 理；另於該吸脫附裝置（1〇)之上游端設置一用以升溫之熱 交換器（30)，俾以將導入該吸脫附裝置（1〇)之待淨化廢氣 適度加熱，而查閱濕度表可清楚得知，升溫之結果會致使 相對濕度下降，亦即該熱交換器（3〇)之設置可提升該吸脫 附裝置（10)對有機溶劑之吸附能力。 此外，請參閱第四圖所示，本創作之第二實施例係較 第一實施例增設一熱泵（50)，而進一步將該熱交換器（30) 連結至該熱泵（50)，讓該熱交換器（3〇)與該熱泵（5〇)之冷 凝器進行熱交換，提供該熱交換器（3〇)所必須消耗之熱 能；而該熱泵（50)之運轉狀態及組成結構非為本案之專利 M407096 標的，不再贅述。於是，該熱交換器（30)可藉由該熱泵（50) 穩定調節其升溫程度，而根據待淨化廢氣之溫度與相對濕 度（或露點溫度）調節該熱交換器（30)之升溫程度，俾使導 入該吸脫附裝置（10)之待淨化廢氣，其相對濕度得以維持 在60%RH以下。 再者，請參閱第五圖所示，本創作之第三實施例係較 第二實施例增設一洗滌器（40)，該洗滌器（40)設置於該熱 交換器（30)之上游端，用以將廢氣氣流中之微粒濾除乾 淨；然而，若進一步讓洗條水冷卻，該洗蘇器（4 0)則另可 降低廢氣氣流之露點溫度，進而產生除濕之效果；於是， 令該洗滌器（40)與該熱泵（50)連結，讓洗滌水與該熱泵（50) 之蒸發器進行熱交換而冷卻。 因此，由於該熱交換器（30)必須消耗熱能，而該洗滌器 (40)之洗滌水冷卻過程必須散發熱能，故利用該熱泵（50)連 結該熱交換器（30)與該洗滌器（40)，讓該熱交換器（30)與該 洗滌器（40)分別與該熱泵（50)之冷凝器與蒸發器進行熱交 換，俾將該洗滌器（40)之洗滌水冷卻過程所必須散發之熱能 轉換成該熱交換器（30)所必須消耗之熱能，進而節能。 基於如是之構成，本創作針對製程所產生含有有機溶 劑之待淨化廢氣，先藉該洗滌器（40)將廢氣氣流中之微粒 濾除乾淨，且若使用冰水洗滌則可先行除濕，再由該熱交 換器（30)適度加熱，俾使其相對濕度得以維持在60%RH以 下，讓該吸脫附裝置（10)在吸附材吸附能力較佳之環境中 進行吸附程序，乃不會受到天候影響而造成淨化成效不穩 定，且降低微粒堵塞吸附材孔洞之可能性；是以，本創作 ivih-u/U96 具有淨化成效穩定不受天候影響以及延長吸附材使用壽命 之功效。 綜上所述，本創作所揭示之構造，為昔所無，且確能 達到功效之增進，並具可供產業利用性，完全符合新型專 利要件，祈請貴審查委員核賜專利，以勵創新，無任德感。 惟，上述所揭露之圖式、說明，僅為本創作之較佳實 施例，大凡熟悉此項技藝人士，依本案精神範疇所作之修 飾或等效變化，仍應包括在本案申請專利範圍内。 【圖式簡單說明】 第一圖係習知有機溶劑淨化裝置之結構說明圖。 第二圖係活性碳之吸附性能說明圖。 第三圖係本創作第一實施例之結構說明圖。 第四圖係本創作第二實施例之結構說明圖。 第五圖係本創作第三實施例之結構說明圖。 【主要元件符號說明】 (10)吸脫附裝置 (20)淨化裝置 (30)熱交換器 (40)洗滌器 (50)熱泵M407096 The purification effect is unstable. According to the working principle of the heat pump, the compressor continuously sucks and compresses the cold coal, so that the refrigerant is assisted in the closed system (4) the phase change of the clothing, and the heat of the environment is absorbed by the evaporator, and the condenser will The cold water is heated into hot water; the energy consumed is the electric energy consumed by the compressor to maintain the refrigerant circulation, so according to the law of energy invariance: the heat energy output from the condenser = the electric energy input to the compressor + the heat energy absorbed by the evaporator from the environment. According to the waste an towel, there are usually particles that cannot be filtered by the money net. These particles will block the pores of the activated carbon or the adsorption material such as the Buddha stone, and reduce the adsorption capacity of the adsorption material, and the particles are blocked. After the pores of the adsorbent material are difficult to remove, the suction (4) causes the life of the material to be shortened. [New content] The main purpose of this creation is to solve the problem that the prior art is susceptible to weather and the purification effect is unstable, and the purification effect is stable and unaffected by the weather. Another purpose of this creation is to save energy. Another purpose of this creation is to extend the useful life of the absorbent material. In order to achieve the above-mentioned effects, the structural feature of the present invention is that the process to produce a waste gas containing an organic solvent to be purified is introduced into a suction-desorption device, and a purification device is disposed at a downstream end of the suction and desorption device, and A heat exchanger for raising the temperature is disposed at the upstream end of the desorption device. Further, a heat pump is further provided to connect the heat exchanger to exchange heat between the heat exchanger and the condenser of the heat pump. Further, no further a scrubber is placed at the upstream end of the heat exchanger. Further, the sacrificial device is further connected to the hot fruit to cool the washing water by heat exchange with the evaporator of the heat system. Moreover, the heat exchanger stably adjusts the degree of temperature rise by the heat pump, and the heat pump adjusts the temperature rise of the heat master according to the temperature and relative humidity (or dew point temperature) of the exhaust gas to be purified. However, the heat exchanger causes the relative humidity of the exhaust gas to be purified introduced into the adsorption and desorption device to be maintained below 60% RH. Alternatively, the suction and detachment device is a fluidized concentrator or a fixed bed concentrator. Further, the purification device is an incinerator, a condenser, a spray chamber or a spray plus ozone chamber. Further, the adsorbent material of the adsorption and desorption device is activated carbon or zeolite. [Embodiment] First, referring to the third embodiment, in the first embodiment of the present invention, the waste gas to be purified containing the organic solvent generated by the process is introduced into a suction and desorption device (10) to treat the exhaust gas. The organic solvent is subjected to a process of adsorption and concentration desorption, and the adsorption and desorption device (10) may be a fluidized concentrator or a fixed bed concentrator; and then a downstream end of the suction and desorption device (10) is provided The purification device (20) further purifies and dehydrates the organic solvent desorbed by the adsorption and desorption device (1〇), and performs purification treatment by incinerator incineration or condenser recovery; and the suction and desorption device (1〇) The upstream end is provided with a heat exchanger (30) for heating, so as to moderately heat the exhaust gas to be purified introduced into the suction and desorption device (1〇), and it is clear from the hygrometer that the result of the temperature rise is caused The relative humidity is lowered, that is, the heat exchanger (3〇) is set to increase the adsorption capacity of the suction and desorption device (10) to the organic solvent. In addition, referring to the fourth figure, the second embodiment of the present invention adds a heat pump (50) to the first embodiment, and further connects the heat exchanger (30) to the heat pump (50). The heat exchanger (3〇) exchanges heat with the condenser of the heat pump (5〇) to provide heat energy that the heat exchanger (3〇) must consume; and the operating state and composition of the heat pump (50) are not The patent of this case, M407096, will not be repeated. Therefore, the heat exchanger (30) can stably adjust the degree of temperature rise by the heat pump (50), and adjust the temperature rise of the heat exchanger (30) according to the temperature and relative humidity (or dew point temperature) of the exhaust gas to be purified. The relative humidity of the exhaust gas to be purified introduced into the suction and desorption device (10) is maintained below 60% RH. Furthermore, referring to the fifth figure, the third embodiment of the present invention adds a scrubber (40) to the second embodiment, and the scrubber (40) is disposed at the upstream end of the heat exchanger (30). For filtering the particles in the exhaust gas stream; however, if the strip water is further cooled, the sacrificial device (40) can further reduce the dew point temperature of the exhaust gas stream, thereby generating a dehumidification effect; thus, The scrubber (40) is coupled to the heat pump (50) to cool the washing water by heat exchange with the evaporator of the heat pump (50). Therefore, since the heat exchanger (30) must consume heat energy, and the washing water cooling process of the scrubber (40) must dissipate heat energy, the heat pump (50) is used to connect the heat exchanger (30) with the scrubber ( 40), the heat exchanger (30) and the scrubber (40) are respectively exchanged with the condenser of the heat pump (50) and the evaporator, and the washing water of the scrubber (40) must be cooled. The heat energy that is dissipated is converted into heat energy that must be consumed by the heat exchanger (30) to save energy. Based on the composition, the creation of the waste gas to be purified containing the organic solvent generated by the process is first filtered by the scrubber (40) to remove the particles in the exhaust gas stream, and if the ice water is used for washing, the dehumidification can be performed first, and then The heat exchanger (30) is moderately heated, and the relative humidity is maintained below 60% RH, so that the adsorption and desorption device (10) performs the adsorption process in an environment in which the adsorption capacity of the adsorption material is better, and the weather is not affected by the weather. The effect of the purification is unstable, and the possibility of the particles blocking the pores of the adsorbing material is reduced; therefore, the ivih-u/U96 has the effect of purifying the stability and being unaffected by the weather and prolonging the service life of the adsorbing material. In summary, the structure revealed by this creation is unprecedented, and it can achieve the improvement of efficacy, and it can be used for industrial utilization. It fully complies with the new patent requirements, and invites your review committee to grant patents. Innovation, no sense of morality. However, the above-mentioned drawings and descriptions are only preferred embodiments of the present invention. Those who are familiar with the art, and the modifications or equivalent changes made in accordance with the spirit of the case should still be included in the scope of the patent application. BRIEF DESCRIPTION OF THE DRAWINGS The first figure is a structural explanatory diagram of a conventional organic solvent purifying apparatus. The second figure is an explanatory diagram of the adsorption performance of activated carbon. The third drawing is a structural explanatory diagram of the first embodiment of the present creation. The fourth drawing is a structural explanatory diagram of the second embodiment of the present creation. The fifth drawing is a structural explanatory diagram of the third embodiment of the present creation. [Explanation of main component symbols] (10) Suction and desorption device (20) Purification device (30) Heat exchanger (40) Scrubber (50) Heat pump