TW202223314A - Drying appartus and drying method - Google Patents
Drying appartus and drying method Download PDFInfo
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- TW202223314A TW202223314A TW109142267A TW109142267A TW202223314A TW 202223314 A TW202223314 A TW 202223314A TW 109142267 A TW109142267 A TW 109142267A TW 109142267 A TW109142267 A TW 109142267A TW 202223314 A TW202223314 A TW 202223314A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/13—Treatment of sludge; Devices therefor by de-watering, drying or thickening by heating
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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
- B01D53/04—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 stationary adsorbents
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- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
- B01J20/3483—Regenerating or reactivating by thermal treatment not covered by groups B01J20/3441 - B01J20/3475, e.g. by heating or cooling
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/001—Drying-air generating units, e.g. movable, independent of drying enclosure
- F26B21/002—Drying-air generating units, e.g. movable, independent of drying enclosure heating the drying air indirectly, i.e. using a heat exchanger
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/06—Controlling, e.g. regulating, parameters of gas supply
- F26B21/08—Humidity
- F26B21/086—Humidity by condensing the moisture in the drying medium, which may be recycled, e.g. using a heat pump cycle
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Abstract
Description
本揭露是有關於一種乾燥設備及乾燥方法,且特別是有關於一種用於如污泥的乾燥設備及乾燥方法。The present disclosure relates to a drying apparatus and drying method, and more particularly, to a drying apparatus and drying method for eg sludge.
待處理廢物(如污泥之廢料)產量逐年增加,我國每年約有上百萬噸污泥處理量,而污泥處理隨之帶來廢氣與乾燥廢熱之排放影響環境的問題。現行的污泥處理設備存在處理過程中所產生的高耗電量,造就高額的運行費用而推廣不易,使合法污泥處理場址減少,污泥清運處理成本亦不斷攀升。因此,亟需提出一種新的乾燥設備,以改善當前存在的問題。The output of waste to be treated (such as sludge waste) is increasing year by year. There are about one million tons of sludge treated in my country every year, and the sludge treatment will bring about the problem of emission of waste gas and drying waste heat that affects the environment. The current sludge treatment equipment has high power consumption during the treatment process, resulting in high operating costs and it is not easy to promote, reducing the number of legal sludge treatment sites, and the cost of sludge removal and treatment is also rising. Therefore, there is an urgent need to propose a new drying device to improve the current problems.
本揭露的目的在於提供一種密閉循環式且低耗能的乾燥設備及乾燥方法。The purpose of the present disclosure is to provide a closed-cycle drying device and a drying method with low energy consumption.
根據本揭露實施例,本揭露提出一種乾燥設備。乾燥設備包括一吸附元件、一氣對氣熱交換器、一冷卻器以及一熱泵系統。吸附元件具有彼此相對的一第一側和一第二側。氣對氣熱交換器氣密連通於吸附元件的第一側。冷卻器氣密連通於氣對氣熱交換器與吸附元件的第一側之間。熱泵系統包括至少二冷凝器及一蒸發器。至少二冷凝器氣密連通於吸附元件的第二側,且至少二冷凝器包括一第一冷凝器和一第二冷凝器。蒸發器氣密連通於氣對氣熱交換器。在乾燥設備中,第一冷凝器用以供一氣體通過,吸附元件用以供通過第一冷凝器的氣體自吸附元件的第二側通過,冷卻器用以供自吸附元件的第二側通過吸附元件的氣體通過,氣對氣熱交換器用以供通過冷卻器的氣體沿一第一流動方向通過,蒸發器用以供沿第一流動方向通過氣對氣熱交換器的氣體通過,氣對氣熱交換器更用以供通過蒸發器的氣體沿一第二流動方向通過,吸附元件更用以供沿第二流動方向通過氣對氣熱交換器的氣體自吸附元件的第一側通過,第二冷凝器用以供自吸附元件的第一側通過吸附元件的氣體通過,以使通過第二冷凝器的氣體對一待處理物進行乾燥處理並回流通過第一冷凝器,以完成循環運作。According to an embodiment of the present disclosure, the present disclosure provides a drying apparatus. The drying equipment includes an adsorption element, an air-to-air heat exchanger, a cooler and a heat pump system. The adsorption element has a first side and a second side opposite to each other. The air-to-air heat exchanger is in airtight communication with the first side of the adsorption element. The cooler is in airtight communication between the air-to-air heat exchanger and the first side of the adsorption element. The heat pump system includes at least two condensers and an evaporator. At least two condensers are airtightly communicated with the second side of the adsorption element, and the at least two condensers include a first condenser and a second condenser. The evaporator is in airtight communication with the air-to-air heat exchanger. In the drying equipment, the first condenser is used for passing a gas, the adsorption element is used for passing the gas passing through the first condenser from the second side of the adsorption element, and the cooler is used for passing the adsorption element from the second side of the adsorption element The gas passing through the air-to-air heat exchanger is used for passing the gas passing through the cooler along a first flow direction, and the evaporator is used for passing the gas passing through the gas-to-air heat exchanger along the first flow direction, and the gas-to-gas heat exchange The evaporator is further used for the gas passing through the evaporator to pass along a second flow direction, the adsorption element is further used for the gas passing through the gas-to-gas heat exchanger in the second flow direction to pass from the first side of the adsorption element, and the second condensate The condenser is used for the gas passing through the adsorption element from the first side of the adsorption element to pass through, so that the gas passing through the second condenser can dry a to-be-treated product and return to the first condenser to complete the circulation operation.
根據本揭露另一實施例,提出一種乾燥方法。乾燥方法可應用於一乾燥設備。乾燥設備包括一吸附元件、一氣對氣熱交換器、一冷卻器以及一熱泵系統,吸附元件具有彼此相對的一第一側和一第二側,熱泵系統包括一第一冷凝器、一第二冷凝器以及一蒸發器。乾燥方法包括以下步驟:將一氣體通過第一冷凝器;將通過第一冷凝器的氣體自吸附元件的第二側通過吸附元件;將自吸附元件的第二側通過吸附元件的氣體通過冷卻器;將通過冷卻器的氣體沿一第一流動方向通過氣對氣熱交換器;將沿第一流動方向通過氣對氣熱交換器的氣體通過蒸發器;將通過蒸發器的氣體沿一第二流動方向通過氣對氣熱交換器;將沿第二流動方向通過氣對氣熱交換器的氣體自吸附元件的第一側通過吸附元件;將自吸附元件的第一側通過吸附元件的氣體通過第二冷凝器;以及使通過第二冷凝器的氣體對一待處理物進行乾燥處理並回流通過第一冷凝器,以完成循環運作。According to another embodiment of the present disclosure, a drying method is provided. The drying method can be applied to a drying apparatus. The drying equipment includes an adsorption element, an air-to-air heat exchanger, a cooler and a heat pump system, the adsorption element has a first side and a second side opposite to each other, and the heat pump system includes a first condenser, a second condenser and an evaporator. The drying method includes the following steps: passing a gas through a first condenser; passing the gas passing through the first condenser through the adsorption element from the second side of the adsorption element; passing the gas passing through the adsorption element from the second side of the adsorption element through a cooler Pass the gas passing through the cooler through the gas-to-gas heat exchanger along a first flow direction; pass the gas passing through the gas-to-gas heat exchanger along the first flow direction through the evaporator; pass the gas passing through the evaporator along a second flow direction passing the gas passing through the gas-to-gas heat exchanger in the second flow direction from the first side of the adsorption element through the adsorption element; passing the gas passing through the adsorption element from the first side of the adsorption element The second condenser; and the gas passing through the second condenser is used to dry a to-be-treated product and reflux through the first condenser to complete the cycle operation.
透過上述的設備及運作方式可實現用於待處理物乾燥的氣體之循環利用,可降低設備的耗能,且藉由元件之間的氣密式連通可實現一密閉式設備,可避免乾燥過程中產生的臭氣或有毒氣體外洩。Through the above-mentioned equipment and operation method, the gas used for drying the object to be treated can be recycled, the energy consumption of the equipment can be reduced, and a closed equipment can be realized by the air-tight communication between the components, which can avoid the drying process. Odor or toxic gas generated in the leak.
為了對本揭露之上述及其他方面有更佳的瞭解,下文特舉實施例,並配合所附圖式詳細說明如下:In order to have a better understanding of the above-mentioned and other aspects of the present disclosure, the following embodiments are given and described in detail with the accompanying drawings as follows:
請參照第1圖,其繪示本揭露一實施例的乾燥設備100之架構示意圖。乾燥設備100包括一吸附元件110、一氣對氣熱交換器120、一冷卻器130以及一熱泵系統140。吸附元件110具有彼此相對的一第一側111和一第二側112,用以區分為第一側111面向的區域為較低溫冷凝區,而第二側112面向的區域為較高溫乾燥區。氣對氣熱交換器120氣密連通於吸附元件110的第一側111,冷卻器130氣密連通於氣對氣熱交換器120與吸附元件110的第一側111之間。熱泵系統140包括至少二冷凝器及一蒸發器142,熱泵系統140例如但不限於熱流工程中所知的直膨式系統。至少二冷凝器包括第一冷凝器141A和第二冷凝器141B,第一冷凝器141A和第二冷凝器141B氣密連通於第二側112,蒸發器142氣密連通於氣對氣熱交換器120。Please refer to FIG. 1 , which shows a schematic structural diagram of a
所述「氣密連通」一詞係指元件與元件之間的連接係為氣閉的而使氣體不會溢出至外界,由此形成一密閉式的回路系統,其中氣密連通之設置可例如透過熱流工程中常使用的風管達成。或者,透過乾燥設備100可選擇性包括一腔體160,腔體160可分割為多個子封閉室分別供各元件容置,並於各子封閉室之間形成單一通道以供氣體的內部流通。The term "air-tight communication" means that the connection between the components is air-tight so that the gas will not escape to the outside world, thereby forming a closed loop system, wherein the air-tight communication can be arranged such as It is achieved through air ducts commonly used in heat flow engineering. Alternatively, the
以下將針對本揭露實施例之第1圖的乾燥設備100對一待處理物S進行乾燥處理的循環運作方式,即應用乾燥設備100之乾燥方法進行說明。The following will describe the cyclic operation mode of drying a to-be-processed object S by the
待處理物S(如汙泥之廢料)例如容置於一容器C。第一冷凝器141A用以供一氣體通過。此氣體例如為空氣,其通過待處理物S經由容器C與第一冷凝氣141A之間的氣密路徑D3抵達第一冷凝器141A。具體而言,第一冷凝器141A的用途在於其內設置有傳熱介質(例如冷媒),在傳熱介質由汽化狀態轉換成液化狀態(即所謂冷凝)時釋放熱能給空氣,以利空氣對吸附元件110進行脫附再生。The to-be-treated material S (such as sludge waste) is accommodated in a container C, for example. The
吸附元件110用以供通過第一冷凝器141A的空氣自吸附元件110的第二側112進入並通過。吸附元件110係為具有吸附劑(例如矽膠、氧化鋁、金屬有機框架(MOFs)或沸石等)的材料,在吸附劑的脫附再生過程中吸收熱能及吸附劑的吸附過程中釋放熱能之特性。具體而言,通過第一冷凝器141A的空氣接收了來自冷媒的熱能,可將此熱能對吸附元件110進行脫附再生作用,吸附元件110上的吸附劑脫附再生而吸收空氣的熱能,使空氣的溫度下降,以進入第一側111面向的較低溫冷凝區。在一實施例中,吸附元件110上的吸附劑進行脫附再生之作用時的再生溫度約為40~70℃。The
冷卻器130用以供自第二側112通過吸附元件110的氣體通過。冷卻器130例如是使用常溫液體(例如水)以間接的方式對空氣進行熱交換,使空氣在通過冷卻器130後進行初步的降溫及除濕。The
氣對氣熱交換器120用以供通過冷卻器130的空氣沿第一流動方向D1通過,蒸發器142用以供沿第一流動方向D1通過氣對氣熱交換器120的氣體通過,接著氣對氣熱交換器120再用以供通過蒸發器142的氣體沿第二流動方向D2通過。具體而言,蒸發器142的用途在於其內設置有傳熱介質(例如冷媒),在傳熱介質由液化狀態轉換成汽化狀態(即所謂蒸發)時吸收空氣的熱能,使空氣的溫度下降。由此,基於乾燥設備100中的空氣係不斷地循環流動的,通過蒸發器142的空氣與通過冷卻器130的空氣藉由氣對氣熱交換120提供之互相交叉的第一流動方向D1與第二流動方向D2進行熱交換,使沿第一流動方向D1通過氣對氣熱交換器120的氣體降溫,而沿第二流動方向D2通過氣對氣熱交換器120的氣體升溫。The air-to-
吸附元件110更用以供沿第二流動方向D2通過氣對氣熱交換器120的氣體自其第一側111進入並通過。具體而言,沿第二流動方向D2通過氣對氣熱交換器120的空氣進入吸附元件110,吸附元件110上的吸附劑進行吸附作用而放熱,此吸附作用不僅使空氣在自第一側111通過吸附元件110後溫度再次上升且空氣的相對濕度下降,以進入第二側112面向的較高溫乾燥區。The
第二冷凝器141B用以供自第一側111通過吸附元件110的空氣通過。具體而言,類似於第一冷凝器141A,第二冷凝器141B的用途亦在於其內設置有傳熱介質(例如冷媒),透過在傳熱介質由汽化狀態轉換成液化狀態時釋放熱能給空氣,使空氣升溫且除濕以利進行待處理物S的乾燥處理。The
通過第二冷凝器141B的空氣對待處理物S進行乾燥處理並回流通過第一冷凝器141A。具體而言,通過第二冷凝器141B的空氣可透過乾燥設備100更包括的一風機150進入容器C中對待處理物S進行乾燥處理,隨後乾燥待處理物S完的空氣回流至第一冷凝器141A,以完成循環運作。此外,在一實施例中,乾燥待處理物S完的空氣在回流至第一冷凝器141A前,可先行通過乾燥設備100選擇性包括的一洗滌元件(未繪示)進行預洗滌,此洗滌元件可設置於第一冷凝器141A的上游,將乾燥待處理物S完的空氣中的粉塵或有毒雜質等過濾出,以淨化空氣。The air passing through the
請參照第2~3圖,第2圖繪示本揭露實施例的乾燥設備的另一實施態樣之架構示意圖,第3圖繪示本揭露實施例的乾燥設備100再一實施態樣之架構示意圖。Please refer to FIGS. 2 to 3. FIG. 2 shows a schematic diagram of the structure of another implementation of the drying apparatus according to the disclosed embodiment, and FIG. 3 shows the structure of another implementation of the
第2圖所示之乾燥設備的另一實施態樣,其與第1圖主要差異在於將乾燥設備100更包括額外蒸發器142A,額外蒸發器142A氣密連通於該第一冷凝器141A,額外蒸發器142A的用途於供對待處理物S進行乾燥處理並沿氣密路徑D3回流的空氣通過,第一冷凝器141A則供通過額外蒸發器142的氣體通過。其中,本實施態樣的乾燥設備100可更包括風機150A以及另一腔體160A,第二冷凝器141B可變更設置於腔體160A中,透過風機150A將自第一側111通過吸附元件110的空氣沿一氣密路徑送至第二冷凝器141B,再透過風機150將空氣對待處理物S進行乾燥處理,同樣可以完成乾燥處理之循環運作。第2圖之實施態樣的優點在於:透過額外蒸發器142A對乾燥處理後的空氣在腔體160A中先進行初步除濕,而後再於腔體160中進行進一步的深度之空氣處理,可提高乾燥處理之運作效率。Another embodiment of the drying apparatus shown in FIG. 2, the main difference from FIG. 1 is that the
第3圖所示之乾燥設備的再一實施態樣,其與第2圖主要差異在於將乾燥設備100更包括額外冷卻器130A,氣密連通於額外蒸發器142A,額外蒸發器142A氣密連通於額外冷卻器130A與第一冷凝器141A之間,其中額外冷卻器130A用以供對待處理物S進行乾燥處理並回流的空氣通過並流向額外蒸發器142A。第3圖之實施態樣的優點在於:可用於高溫乾燥待處理物S(例如用於乾燥待處理物S的空氣溫度約為70℃以上)之狀況,乾燥待處理物S完的空氣回流的溫度也隨之提高,因此需要加裝設置一額外冷卻器130A以對回流的空氣在腔體160A中做一次降溫,再透過額外蒸發器142A對空氣在腔體160A中進行除濕,而後再於腔體160中進行進一步的深度之空氣處理。Another embodiment of the drying apparatus shown in FIG. 3, the main difference from FIG. 2 is that the drying
請參照第4圖,第4圖繪示一比較例態樣的乾燥設備200之架構示意圖。此乾燥設備200之比較例係僅透過熱泵系統240的冷凝器241與蒸發器242進行乾燥待處理物S後的空氣進行處理,蒸發器242用以對空氣進行降溫除濕,接著冷凝器241用以對空氣加熱使空氣乾燥升溫,而再次進入容器C中對待處理物S進行乾燥,由此完成循環運作。相較於本揭露第1~3圖的實施例態樣,第4圖所示之乾燥設備200缺少了吸附元件、氣對氣熱交換器及冷卻器的設置,而無法透過此些元件利用到熱泵系統240運作產生的廢熱進行回收。經實驗分析後,本揭露使用熱泵系統140、吸附元件110、氣對氣熱交換器120及冷卻器130的乾燥設備100,相較於僅使用熱泵系統240的乾燥設備200可將廢熱回收再利用,從而能效指標可提升約20~30%,且污泥的乾燥時間縮短約30%,總耗電量降低約30%,具有顯著性的改善效果。在一特定實施例以汙泥為例,在乾燥溫度(50℃)除濕率8(g/s)。在另一特定實施例,在乾燥溫度(70℃)除濕率18(g/s)。這裡指的乾燥溫度就是冷凝器出口的溫度。Please refer to FIG. 4 . FIG. 4 illustrates a schematic structural diagram of a
請參照第5A~5B、6A~6B圖,第5A~5B、6A~6B圖分別繪示本揭露實施例的乾燥設備100的吸附元件110不同態樣的示意圖。吸附元件110可例如為具有吸附劑之一轉輪。吸附元件110具有供通過第一冷凝器141A的空氣通過的脫附再生區域Z2、以及供沿第二流動方向D2通過氣對氣熱交換器120的空氣通過的吸附區域Z1。如第5A圖所示,在一實施例中,吸附區域與脫附再生區域的面積比可為1:1,兩區域的面積相同。如第5B圖所示,在一實施例中,吸附區域Z1與脫附再生區域Z2的面積比可為3:1,可在同樣轉輪體積之下增加處理風量,且可透過操作參數調整使除濕能力差距不大。此外,吸附元件110可更設置具有一冷卻區域Z3。如第6A圖所示,在一實施例中,吸附區域Z1、脫附再生區域Z2與冷卻區域Z3的面積比為1:1:1,透過增加冷卻區域Z3,可以使效率提升30%。如第6B圖所示,在一實施例中,吸附區域Z1、脫附再生區域Z2與冷卻區域Z3的面積比為3:1:1。吸附區域與再生、冷卻面積指的是轉輪的比例,吸附完後轉輪上的吸附劑會飽和,所以需要進行再生,而再生完成後,轉輪上的吸附劑會很熱,如果先透過冷卻區稍微降溫,可以加強吸附區的吸附能力。Please refer to FIGS. 5A-5B and 6A-6B. FIGS. 5A-5B and 6A-6B are schematic diagrams of different aspects of the
在一特定實施例,轉輪須放在蒸發器之後,確保轉輪的吸附除溼能力維持高效率。In a specific embodiment, the runner must be placed after the evaporator to ensure that the adsorption and dehumidification capacity of the runner maintains high efficiency.
本揭露使用熱泵系統、吸附元件、氣對氣熱交換器及冷卻器的設置促使乾燥設備內可利用溫度及濕度梯度差,即便僅使用單顆風機的情況下,在密閉式達到冷熱源回收完成吸附元件之吸附及再生,另一方面,系統中透過氣對氣熱交換器作用,更能使濃縮的水氣易被冷凝排出系統,達到乾燥的目的。The present disclosure uses a heat pump system, an adsorption element, an air-to-air heat exchanger and a cooler to make use of the temperature and humidity gradient differences in the drying equipment. Even if only a single fan is used, the recovery of cold and heat sources can be achieved in a closed type. The adsorption and regeneration of the adsorption element, on the other hand, the effect of the permeate gas-to-air heat exchanger in the system can make the concentrated water vapor easily condensed and discharged from the system to achieve the purpose of drying.
綜上所述,雖然本揭露已以實施例揭露如上,然其並非用以限定本揭露。本揭露所屬技術領域中具有通常知識者,在不脫離本揭露之精神和範圍內,當可作各種之更動與潤飾。因此,本揭露之保護範圍當視後附之申請專利範圍所界定者為準。To sum up, although the present disclosure has been disclosed above with embodiments, it is not intended to limit the present disclosure. Those with ordinary knowledge in the technical field to which the present disclosure pertains can make various changes and modifications without departing from the spirit and scope of the present disclosure. Therefore, the scope of protection of the present disclosure should be determined by the scope of the appended patent application.
100,200:乾燥設備
110:吸附元件
111:第一側
112:第二側
120:氣對氣熱交換器
130:冷卻器
130A:額外冷卻器
140,240:熱泵系統
141A:第一冷凝器
141B:第二冷凝器
142,242:蒸發器
142:額外蒸發器
150,150A:風機
160,160A:腔體
241:冷凝器
C:容器
D
1:第一流動方向
D
2:第二流動方向
D
3:氣密路徑
S:待處理物
Z
1:吸附區域
Z
2:脫附再生區域
Z
3:冷卻區域
100, 200: drying plant 110: adsorption element 111: first side 112: second side 120: air-to-air heat exchanger 130: cooler 130A: additional cooler 140, 240:
第1圖繪示本揭露實施例的乾燥設備100之架構示意圖。
第2圖繪示本揭露實施例的乾燥設備100的另一實施態樣之架構示意圖。
第3圖繪示本揭露實施例的乾燥設備100的再一實施態樣之架構示意圖。
第4圖繪示比較例態樣的乾燥設備之架構示意圖。
第5A~5B、6A~6B圖分別繪示本揭露實施例的乾燥設備的吸附元件不同態樣的示意圖。
FIG. 1 is a schematic structural diagram of a
100:乾燥設備 100: Drying equipment
110:吸附元件 110: Adsorption element
111:第一側 111: First side
112:第二側 112: Second side
120:氣對氣熱交換器 120: Air-to-air heat exchanger
130:冷卻器 130: Cooler
140:熱泵系統 140: Heat Pump Systems
141A:第一冷凝器 141A: First condenser
141B:第二冷凝器 141B: Second condenser
142:蒸發器 142: Evaporator
150:風機 150: Fan
160:腔體 160: cavity
C:容器 C: container
D1:第一流動方向 D 1 : The first flow direction
D2:第二流動方向 D 2 : Second flow direction
D3:氣密路徑 D 3 : Airtight Path
S:待處理物 S: to be processed
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SE8100042L (en) * | 1981-01-07 | 1982-07-08 | Technoscript Ab | METHOD AND DEVICE FOR DRYING MATERIALS IN A DRYER |
KR100947616B1 (en) * | 2008-05-22 | 2010-03-15 | 엘지전자 주식회사 | Dehumidifying air conditioner |
TWI351500B (en) * | 2008-12-03 | 2011-11-01 | Ind Tech Res Inst | Low power dehumidifier |
CN101749814B (en) * | 2008-12-12 | 2012-08-08 | 财团法人工业技术研究院 | Dehumidification device with low power consumption |
CN103827589B (en) * | 2011-09-29 | 2016-10-19 | 大金工业株式会社 | Dehumidification system |
CN202778221U (en) * | 2012-06-20 | 2013-03-13 | 马军 | Vapor compression type heat pump and runner adsorption and dehumidification coupled operation drying machine |
AU2013354898B2 (en) * | 2012-12-05 | 2017-09-14 | Commonwealth Scientific And Industrial Research Organisation | Compact desiccant cooling system |
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CN103090484B (en) * | 2013-01-18 | 2015-08-05 | 清华大学 | A kind of humiture independence control air conditioner system and using method thereof |
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CN203803339U (en) * | 2014-01-22 | 2014-09-03 | 马军 | Compress-type heat pump and runner adsorbing dehumidifying coupling running low-temperature dryer |
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