201240922 六、發明說明： 【發明所屬之技術領域】 本發明是涉及一種螺旋式多效蒸餾系統，能利用熱能 [如：太陽熱能]，使水[海水、污水、欲淨化的水]蒸發為水蒸 氣，再將水蒸氣冷凝還原成乾淨的蒸顧水，是屬於淨水設備、 海水淡化、廢水回收、太陽能應用等的專業領域。 【先前技術】 擴散式多效蒸I留系統為一高效率的熱驅動式蒸顧水製作 系統，是由Cooper與Appleyard，於西元1967年所提出[P.I.201240922 VI. Description of the Invention: [Technical Field] The present invention relates to a spiral multi-effect distillation system capable of evaporating water [sea water, sewage, water to be purified] into water by utilizing thermal energy [eg, solar thermal energy] Vapor, and then condense water vapor into a clean steaming water, is a professional field of water purification equipment, desalination, wastewater recycling, solar energy applications. [Prior Art] The diffusion type multi-effect steaming I stay system is a high-efficiency heat-driven steaming water production system, which was proposed by Cooper and Appleyard in 1967. [P.I.
Cooper and J.A. Appleyard. Sun at Work 12 (1967) P4] 〇 如圖1所示為傳統擴散式多效蒸餾系統的原理示意圖。其 中’傳統擴散式多效蒸餾系統，其主要包含：一傳統供熱裝置 (A)、一傳統補水裝置(B)、及數片層迭的傳統蒸餾片（c)。 當中最重要結構為傳統蒸餾片（C)，傳統蒸餾片（c)為薄片 狀，其中一面為平滑表面，是作為傳統冷凝面(α)，好讓水蒸 氣可以在此凝結，傳統冷凝面(C1)下側設有傳統集水溝， 可收集由前述傳統冷凝面(C1)上，水蒸氣(HW)所凝結而滴落 的蒸餾水(DW); 、而另一面緊貼一層作為傳統蒸發片（C2)的毛細材料，傳統 補水裝置(B)供應4寺洛顧的水(w)，由傳統蒸發片（C2)吸收後， 在此吸熱蒸發； 傳統蒸館片（c)的層送方式，為以一傳統冷凝面(ci)面對 另-傳統純片（c)的傳統蒸發片（C2)的方式層送，且邊線對 齊、近距間隔平行排列； 、 -側最靠外的傳統冷凝面(C1)，緊靠傳統供絲置 傳統供熱裝置⑷為利用外來熱源[如1陽能、水蒸氣]的熱能 (P)，加熱鄰近的傳統蒸餾片(C)，故此傳統蒸則(C)的溫度為 201240922 附于傳統蒸發片（(：2)上的水(w)，吸收熱能(p)、蒸發 :、、'水洛氣(HW) ’水蒸氣(HW)擴散至對面傳統蒸餾片⑹的傳統 冷凝面(ci)上，凝結成蒸鶴水(DW); 、、士此同時，前述凝結過程中所放出的潛熱[Latent Heat]， 成為每片傳統蒸餘片(q的熱源，傳導至另一鄰近的傳統蒸發 片（C2)上，使其所含的水(w)蒸發，如此重複蒸餾過程，直至 最後-片傳統蒸館片(C)，再將熱量排出系統，故最後一片傳 統蒸餾片（C)處，溫度為最低。 【發明内容】 一、 本發明所欲解決的問題： —傳統擴散式多效蒸齡、統中，蒸㈣應用了毛細材料，作 為洛發片來使用’以達到吸附水、並讓水蒸發、最後獲得蒸德 水的效果’但疋丈到毛細材料的影響，整個系統經過一段時日 的運作後，毛細材必因水中雜質的污染，而漸漸失去作用，必 須要更換蒸餾片，才能繼續的運作。 但是，因為傳統擴散式多效蒸餾系統，各個部件緊密配 合’結構過於複雜緊凑’造成元件損耗後拆換不易，並且需要 絕熱部位較多，機體許多ϋ積被保溫材料佔據，故[產量/體積 比]較小」形成此傳統擴散式多效蒸館系統，製作成本和維護 成本偏高’無法普及的原因。 〜鑑於此’如何讓此種效率優良的擴散式多效蒸鶴系統， 得以貫用化’降低製作成本和維護成本，以使其普及化，便成 為本發明欲改進的目的。 二、 本發明的技術手段： 本發明目的在於提供-種低成本、結構㈣、生產與維護 方便、能製作蒸餾水的螺旋式多效蒸餾系統。 一為，決前述問題及達到本發明的目的，本發明技術手段， 4 201240922 為二種螺旋式多效蒸餾系統，其包括： 祕系統(100) ’該蒸館系統(1〇〇)是 飽中心處的供熱裝置(2)、以及一 2蒸 餾表置⑴頂端處的補水裝置(3)所組成； 其特徵在於： 所述洛館裝置⑴是由一片螺旋蒸鶴片（11)所組成； 、t 〇亥螺％祕片（11)為呈薄片狀，其一面為供水蒸氣(HW) 凝冷凝面(12) ’且另—面為作為蒸發用的蒸發面⑴广 S亥洛發面(13)緊貼有一片以毛細材料所制而成、作為蒸發 用的螺旋蒸發片（131)，並且來自補水裝 (w):能被吸附於該螺旋蒸發片（131)上； «亥螺疑蒸顧片（11)為從供熱裝置⑺處，以冷凝面⑽、蒸 發面(U)的順序，以一間隔(M)往遠離供熱裝置⑵的方向、^ 螺旋排列設置，且螺旋蒸则⑴)的頂端與底端為呈封閉狀， 以防止水蒸氣(HW)外泄； 在冷凝面(12)下方，有一供收集由冷凝面(12)滴落之蒸餾 水(DW)用的螺旋集水溝(15); 藉由供熱裝置(2)提供熱能(P)，讓熱能(p)由螺旋蒸餾片 (11)之最内側圈處的冷凝面(12)處，往外傳導至此冷凝面(12) 相對的蒸电面(13)處’再傳導至與此蒸發面⑴)緊貼的螺旋蒸 發片（131)上，讓此處螺旋蒸發片（丨31)所吸附的水(w)，受熱能 (P)蒸發為水蒸氣(HW) ’而此水蒸氣(HW)擴散至位於下一圈處 的冷凝面(12)上時、會凝結成蒸餾水(DW)，此時，水蒸氣(HW) 凝結為蒸餾水(DW)的過程中、所放出的潛熱，會往外傳導至 此冷凝面(12)相對的蒸發面(13)處，再傳導至與此蒸發面(13) 緊貼的螺旋蒸發片（131)上，又使此處螺旋蒸發片⑴丨)所吸附 的水(W)，蒸發為水蒸氣(HW)，同樣，水蒸氣(HW)會擴散至 位於下一圈處的冷凝面(12)上、以凝結成蒸顧水(Dw)，如此重 201240922 複蒸餾過程' 直至蒸餾系統(100)之螺旋蒸餾片（11)的最外側 圈、最遠離供熱裝置(2)處，以將熱量排出至蒸餾系統(1〇〇)外。 根據上述的螺旋式多效蒸餾系統，所述供熱裝置(2)，為 呈柱狀設置，具有一供熱面(21)，該供熱面(21)的表面，與相 鄰螺旋蒸餾片（11)的冷凝面(12)間，更覆蓋設有一環狀蒸發片 (22) ’補水裝置同時對此環狀蒸發片（22)由上方補水，該供熱 面(21)能將進入供熱裝置(2)的外來任一型式的能量，轉換成為 熱能後、經由供熱面(21)傳導至環狀蒸發片（22)，使環狀蒸發 片（22)上的水蒸發，水蒸汽擴散凝結於螺旋蒸餾片⑴)之最内 侧圈處的冷凝面(12)上； 而所述環狀蒸發片（22)，其是為下列之一：單獨設置的型 式、和螺旋蒸發片（131)為一體設置的型式。 根據上述的螺旋式多效蒸餾系統，所述供熱裝置(2)，是 為一流體谷器(23),且流體容器(23)與供熱面(21)、具有良好的 熱接觸、或是同為一體； 而所述流體谷器(23)，設有一能供導引任一型式之流體狀 熱媒(HC)、流至供熱面(21)背面、使熱媒(HC)所含之熱能(p)、 能傳導至供熱面(21)、以被蒸餾裝置(1)帶走用的輸入管(24); 以及 * 一能導引前述被取熱後之熱媒(HC)離開的輸出管(25)。 根據上述的螺旋式多效蒸餾系統，所述供熱裝置的供 熱面(21)，更設有—電熱裝置(28)，該電熱裝置⑽將電能轉換 為熱能，以透過供熱面(；21)傳送至蒸餾裝置〇)。 根據上述的螺旋式多效蒸顧系統，所述供熱裝置(2)，是 由-設於該蒸館裝置⑴中心處、並將蒸镏裝置⑴封閉 = 塞體(26);以及 一能將蒸汽輸入蒸鶴裝置⑴内的蒸汽輸入管⑼所組成。 根據上述的螺旋式多效蒸餾系統，所述補水裝置(3)，具 6 201240922 有至〆個裝盛有待蒸餾之水(w)的水槽(31)、及至少一個以 毛細材料所製成的補水體(32)，且該補水體(32)的—端、浸泡 於水槽(31)⑽水(W)中’並另―端與螺旋蒸發片（131)頂端連 接，能將水(w)由水槽⑼處、引入螺旋蒸發片（131)中； 、而所述補水體(32)，其是為下列之一：可單獨拆換的型 式、和螺旋蒸發片（131)為一體設置的型式。 根據上述的螺旋式多效蒸餾系統，所述螺旋蒸館片⑴）， 其每-圈之_邊賴’為呈下列之—的狀態：由關至外側 而緩緩變低、由内側至外側而皆等高、由内側至外側而緩緩變 高。 根據上述的螺旋式多效蒸顧系統，所述蒸餾系統(灣 中’更包括-能將蒸餾水所含之餘熱，用以預熱待蒸館之水(w) 的熱回收裝置(4); 所述熱回收裝置(4)，是包括一第一回熱管(41); 又所述第-回熱管⑼的巾間段，為設置於螺旋集水溝 (15)内、或與螺旋集水溝(15)内之蒸鶴水(腹)具有良好的孰接 觸’而第一回熱管(41)的兩端分別為待蒸顧之水(W)之輸入端 和輸出端； 由輸入端進入第—回熱管⑷）的待蒸餾之水(w)，在經過 中間段及收螺疑集水溝(μ)内蒸顧水(Dw)内多餘之敎能(p) 後，再由輸出端離開傳送至補林置(3)。 ' 根據上述的螺旋式多效蒸鶴系統，所述蒸顧系統(1〇〇) 中’更包括-能將蒸館系統(1〇騎產生之廢水(sw)，其内所 含之餘熱’用以預熱待蒸镏之水(W)的熱回收裝置(4); 所述熱回收裝置(4)，是包括一第二回熱管(42); 又所述第二回熱管(42)的中間段，為設置於螺旋蒸發片 (13.1)下ir而、並與由螺旋蒸發片（131)排出之廢水(sw)具有良好 的熱接觸’而第二回熱管(42)的兩端，分別為待蒸鶴之水(w) 201240922 之輸入端和輸出端； =輸人端進人第二回熱管(42)的待蒸顧之水(w)，在經過 又吸收由螺旋蒸發片（131)排出之廢水(SW)之多餘之熱能 ^再由輪出端離開傳送至補水裝置(3)。 ，據上述的螺旋式多效蒸顧系統，所述蒸顧系統⑽) 包括—平行於螺旋蒸㈣（11)之軸心、垂直設置於螺旋 ，(11)内、能將螺旋蒸館片⑴)處之各間隔㈤分隔、以形 成數個區域(S)的分隔條(9)。 二、對照先前技術之功效： 1.為了讓此觀率優良的職式多效蒸餾祕，得以實 用化’本發明提出將螺旋式多效蒸館系統模組化設計之概令. i 統 =)分為三個部件，分別為：蒸餾裝置⑴、供熱 、（）補水#置(3)，蒸館裝置⑴包含一片螺旋蒸館片，以 置⑶之水’加上來自供熱裝置_熱能，將水Cooper and J.A. Appleyard. Sun at Work 12 (1967) P4] 〇 Figure 1 shows the schematic diagram of a conventional diffusion multi-effect distillation system. Among them, the conventional diffusion multi-effect distillation system mainly comprises: a conventional heating device (A), a conventional water replenishing device (B), and a plurality of laminated conventional distillation sheets (c). The most important structure is the traditional distillation sheet (C), the traditional distillation sheet (c) is flaky, one side of which is a smooth surface, which is used as a conventional condensation surface (α), so that water vapor can be condensed here, the conventional condensation surface ( C1) The lower side is provided with a traditional water collecting ditch, which can collect distilled water (DW) which is dripped by water vapor (HW) on the aforementioned conventional condensation surface (C1); and the other side is closely attached to the layer as a conventional evaporation sheet. The capillary material of (C2), the traditional water supply device (B) supplies the water (w) of 4 Temple Luogu, absorbed by the traditional evaporation sheet (C2), and absorbs heat and evaporates here; the layering method of the traditional steaming piece (c) , layered in the manner of a conventional evaporation sheet (C) facing a conventional evaporation sheet (C2) of the other conventional pure sheet (c), and the side lines are aligned and closely spaced in parallel; and the side is the outermost tradition Condensation surface (C1), close to the traditional wire supply conventional heating device (4) is to use the external heat source [such as 1 cation, water vapor] thermal energy (P), heating the adjacent traditional distillation plate (C), so the traditional steaming (C) The temperature is 201240922 attached to the traditional evaporation sheet ((:2) on water (w), absorption of thermal energy (p), evaporation:,,] (HW) 'Water vapor (HW) diffuses to the traditional condensation surface (ci) of the opposite conventional distillation sheet (6) and condenses into steamed crane water (DW); and, at the same time, the latent heat released during the above condensation process [Latent Heat] ], become the heat source of each piece of traditional steaming sheet (q, conduction to another adjacent traditional evaporation sheet (C2), causing the water (w) contained therein to evaporate, thus repeating the distillation process until the last-piece conventional steaming In the museum piece (C), the heat is discharged out of the system, so the temperature is the lowest at the last piece of the conventional distillation piece (C). [Summary of the Invention] 1. Problems to be solved by the present invention: - Traditional diffusion type multi-effect steaming age, In the system, steaming (4) applied capillary material, as a Luofa tablet to use 'to achieve adsorption of water, and let the water evaporate, and finally get the effect of steaming water' but the effect of the hair to the capillary material, the entire system after a period of time After the operation, the capillary material will gradually lose its effect due to the contamination of impurities in the water, and the distillation piece must be replaced in order to continue the operation. However, because of the traditional diffusion multi-effect distillation system, the various components are closely matched with the structure being too complicated and compact. ' After the component is lost, it is not easy to replace and replace, and more insulation parts are needed. Many of the body's hoarding is occupied by the thermal insulation material, so the [yield/volume ratio] is small. This traditional diffusion multi-effect steaming system is formed, and the manufacturing cost and maintenance cost are formed. The reason why it is too high is not popular. ~ In view of this, how to make this kind of efficient diffusion type multi-effect steaming crane system can be used to reduce the production cost and maintenance cost to make it popular. The object of the invention is as follows: 2. The technical means of the invention: The object of the invention is to provide a spiral multi-effect distillation system with low cost, structure (four), convenient production and maintenance, and capable of producing distilled water. OBJECT OF THE INVENTION, the technical means of the present invention, 4 201240922 are two kinds of spiral multi-effect distillation systems, including: secret system (100) 'The steaming system (1〇〇) is a heating device at the center of the saturate (2) And a water replenishing device (3) at the top of the distillation table (1); characterized in that: the Luoguan device (1) is composed of a piece of spiral steamed crane piece (11); The sheet (11) is in the form of a sheet, one side of which is a water vapor (HW) condensation surface (12)' and the other side is an evaporation surface for evaporation (1). Made of capillary material, used as a spiral evaporation sheet (131) for evaporation, and from hydration equipment (w): can be adsorbed on the spiral evaporation sheet (131); «Hailu suspected steam film (11) is From the heating device (7), in the order of the condensation surface (10) and the evaporation surface (U), at a distance (M) away from the heating device (2), spirally arranged, and the top and bottom of the spiral steam (1)) The end is closed to prevent water vapor (HW) from leaking; under the condensation surface (12), there is a spiral sump (15) for collecting distilled water (DW) dripping from the condensation surface (12); The heat energy (P) is supplied by the heating device (2), and the heat energy (p) is conducted from the condensation surface (12) at the innermost ring of the spiral distillation piece (11) to the opposite side to the steaming surface (12). The electric surface (13) is 'reconducted to the spiral evaporation sheet (131) which is in close contact with the evaporation surface (1), and the water (w) adsorbed by the spiral evaporation sheet (丨31) is heated (P). Evaporation to water vapor (HW 'When this water vapor (HW) diffuses to the condensation surface (12) located at the next turn, it condenses into distilled water (DW), at which time the water vapor (HW) condenses into distilled water (DW). The latent heat released is conducted to the opposite evaporation surface (13) of the condensation surface (12), and then transmitted to the spiral evaporation sheet (131) which is closely attached to the evaporation surface (13), and the spiral is made here. The water (W) adsorbed by the evaporation sheet (1) is evaporated to water vapor (HW). Similarly, the water vapor (HW) is diffused to the condensation surface (12) located at the next turn to condense into steam. (Dw), so heavy 201240922 double distillation process 'up to the outermost circle of the spiral distillation piece (11) of the distillation system (100), farthest from the heating device (2) to discharge heat to the distillation system (1〇〇 )outer. According to the above-described spiral multi-effect distillation system, the heating device (2) is arranged in a column shape, has a heating surface (21), a surface of the heating surface (21), and an adjacent spiral distillation sheet. Between the condensation surface (12) of (11), an annular evaporation sheet (22) is further covered with a water replenishing device, and at the same time, the annular evaporation sheet (22) is filled with water from above, and the heating surface (21) can enter the supply surface. Any type of external energy of the heat device (2) is converted into heat energy and then conducted to the annular evaporation sheet (22) via the heating surface (21) to evaporate the water on the annular evaporation sheet (22), and the water vapor The diffusion is condensed on the condensation surface (12) at the innermost ring of the spiral distillation sheet (1)); and the annular evaporation sheet (22) is one of the following: a separately provided pattern, and a spiral evaporation sheet (131) ) The type set as one. According to the above-described spiral multi-effect distillation system, the heating device (2) is a fluid tank (23), and the fluid container (23) has good thermal contact with the heating surface (21), or The fluid trough (23) is provided with a fluid-like heat medium (HC) capable of guiding any type, flowing to the back surface of the heating surface (21), and the heat medium (HC) Inclusive heat energy (p), an input pipe (24) capable of being conducted to the heating surface (21), carried away by the distillation apparatus (1); and * capable of guiding the aforementioned heat medium (HC) ) Leave the output tube (25). According to the above-mentioned spiral multi-effect distillation system, the heating surface (21) of the heating device is further provided with an electric heating device (28), which converts electrical energy into thermal energy to pass through the heating surface (; 21) Transfer to the distillation unit 〇). According to the above-described spiral multi-effect steaming system, the heating device (2) is provided at the center of the steaming device (1), and the steaming device (1) is closed = the plug body (26); The steam is supplied to the steam inlet pipe (9) in the steamer device (1). According to the above-described spiral multi-effect distillation system, the water replenishing device (3) has 6 sinks (31) containing water (w) to be distilled, and at least one made of capillary material. The water replenishing body (32), and the end of the water replenishing body (32) is immersed in the water tank (31) (10) water (W) and is connected to the top end of the spiral evaporation sheet (131) to enable water (w) From the water tank (9), introduced into the spiral evaporation sheet (131); and the water replenishing body (32), which is one of the following: the separately replaceable type and the spiral evaporation sheet (131) are integrally arranged . According to the above-described spiral multi-effect distillation system, the spiral-steamed pavilion (1)) has a state in which each of the turns is in the following state: from the closed to the outer side, gradually decreases from the inside to the outside. They are all equal in height and gradually increase from the inside to the outside. According to the above-mentioned spiral multi-effect steaming system, the distillation system (including the heat recovery device (4) capable of preheating the water (w) of the steaming hall; The heat recovery device (4) includes a first heat recovery pipe (41); and the intermediate portion of the first heat recovery pipe (9) is disposed in the spiral water collection ditch (15) or with the spiral water collection The steamed crane water (abdominal) in the ditch (15) has a good 孰 contact' and the two ends of the first regenerative pipe (41) are respectively the input end and the output end of the water (W) to be distilled; - the water to be distilled (w) of the heat recovery pipe (4), after passing through the intermediate section and the snail collection ditch (μ), the excess energy (p) in the water (Dw) is distilled, and then exits from the output end. Transfer to the patch (3). According to the above-mentioned spiral multi-effect steamed crane system, the steaming system (1〇〇) includes a steaming system (a waste water (sw) generated by the rider, the waste heat contained therein] a heat recovery device (4) for preheating the water (W) to be distilled; the heat recovery device (4) includes a second heat recovery pipe (42); and the second heat recovery pipe (42) The middle section is provided under the spiral evaporation sheet (13.1) and has good thermal contact with the wastewater (sw) discharged from the spiral evaporation sheet (131) and both ends of the second heat recovery tube (42). They are the input and output of the water to be steamed (w) 201240922; = the water to be distilled (w) entering the second heat pipe (42), and then absorbed by the spiral evaporation sheet ( 131) The excess heat energy of the discharged wastewater (SW) is transferred from the wheel outlet to the water supply device (3). According to the spiral multi-effect steaming system described above, the steaming system (10) includes - parallel to The axis of the spiral steaming (4) (11), which is vertically disposed in the spiral, and (11), can separate the intervals (5) at the spiral steaming plate (1)) to form a partition (9) of several regions (S). Second, in accordance with the efficacy of the previous technology: 1. In order to make this view of the multi-effect distillation secret of the job, it is practical to use the invention to propose a modular design of the spiral multi-effect steaming system. i system = ) is divided into three parts, namely: distillation unit (1), heating, () hydration # (3), steaming device (1) contains a spiral steaming piece, to set (3) water 'plus from the heating device _ Heat, water
=過獲取外來熱量的方式，以提供給蒸織置⑴製ί乍H= The way to obtain external heat to provide steam woven (1) system 乍 乍 H
Lit亦t為水分祕之用的熱能來源；補水裝置⑶為透過獲 ，水的方式’以麟蒸叙水，輸送至蒸鱗置⑴處； ^個部件均為各自獨立的系統，可分別拆換維修，蝴牛中所 有的毛細元件，均採用可單獨拆換的型式；此模組化之設計將 使系統在組裝上更為簡便，且元件損耗後拆賴單，可 ^維護成本；尤其祕巾的毛細元件都是胁快速折損之耗 材，右為可輕易皁獨拆換之設計，毛細元件即可拆下 =性='提高系統之使用壽命和降低維護二系統 2.比起傳統擴散式多效蒸餾系統的設計， 少得多，整個蒸齡統⑽)幾乎所有體積，都作為^用， 其他無關讀料的體雜少，蒸齡、统⑽)外部面積，幾 201240922 乎都作為散熱用’散熱面積大增，透過螺旋蒸德片（n)的使用， 越外層面積越大’可提高較外層的熱傅量，故加人熱回收裝置 (，後二不只效率提升’產量也會增加，傳統擴散式多效蒸顧 系統若加入熱回收裝置(4)，雖可提升效率，但會使總產量降 而且相較於傳統擴散式多效蒸館系統，螺旋蒸館片⑴)的 厚度可以更薄，而不易變型，可大大提升熱導率。 3. 本發明中，由於螺旋蒸餾片（u)的形狀，使得蒸餾片的 曲度較大而的擁有較強的結構，故蒸館片厚度可㈣和面積可 更大’故本發明相較於傳統擴散式多效蒸⑽統，具有易輕量 化和大型化的優勢，只需加大直徑和長度。 4. 本發明中，螺旋蒸餾片（11)間的間隔(M)，為一由内到外 相連通的空間，當供熱裝置(2)輸人過多的熱量時，而發生入 熱超載時’蒸汽可直接往散熱面積較大的職蒸制⑴)之外 側圈處擴散聽’轉傳賴散式乡效蒸齡統，會溢出蒸條 片造成浪費。 5. 本發明中’透過螺旋蒸餾片⑼的使用，為一整片從内 到外相連接的m補水的均自度佳，不像傳統擴散式多 效蒸餾系統，有難以均勻補水的問題。 处6·本發明中，透過螺旋蒸餾片（11)的使用，讓供熱裝置(2) 能以圓柱狀為外型，易於製作為耐壓的封閉結構，適用於密閉 式的熱媒循環系統，熱源的利用將更有效率。 /蒸⑽、統(1(H))的最大翻，如：海水淡化，因海水含有 大里雜質溶解其中，為了防止雜質結晶於毛細材料上、使效能 降低，必須不斷加入新海水，並將濃縮之廢水排除，但所排= 之廢水含有大量餘熱，將之直接排除相當可惜；另一方面，本 ，明蒸餾系統(1〇〇)所產生之蒸餾水(Dw)，亦含有大量餘熱， 右热熱水需求，而將之冷卻散熱、亦是浪費此部份熱量； 熱回收裝置(4) ’可㈣統t多餘的熱能(P)，透過熱交換的方 201240922 式，用以預熱待蒸顧的水(w)，或是用來預熱熱媒(HC)，以提 升運作效率。 8·本發明中，透過螺旋蒸餾片（11)的使用，僅需將一整條 回，管設置於集水溝内’透過管喊雜録溝_蒸顧水作 熱父換’即可作為回收蒸顧水餘熱之功能；另僅需將一整條回 熱官，置於祕片下方’透過管内流體與由蒸發片排出的廢水 作熱父換’即可料回收廢水餘熱之功能；故本發明之熱回 裝置(4)的設置’將變得更為簡單，且效率更高。… 曰7¾丨發片（i3i)上流動時’其流速必須適中，若流 ?多=帶走而減低效率;螺旋蒸發片_上的么: :的變動而作變化，通常我們使用的熱_ :么太，]都不疋敏的熱源，同時在不敏 各個部份 難的關鍵技術，-般是將毛細材料一端泡入水中番 桶外，則桶内的水就會因毛細力和重 而垂出 慢慢源源不斷從另一端产出插外 乍用，&者毛細材料 截面積、水平面與毛力、 比’二與水平面和轉析點最高處的距離呈反比;二、= 館片上的毛細材料，伸長到水槽内直接t 2統做法是將蒸 便;另-方面“==裝時較為不 而使得整片毛細材提早失效，更健 =杨開頭處， 發明提出將補水用的毛細材，和須又浪費；本 念；在螺嶋⑽D上_毛細材，作^ 201240922 其底面與螺旋蒸發片（131)頂面相接 觸 端泡入水槽(31)内之水(W)中、另-端與水分配 體亦可分開設置；水(W)由補水體(32)的入水)， ^透至整體’螺旋蒸發片（131)從水分配H(33)底部吸水;°兩 另有為毛細材、— 器(33)頂面接 為一整 邊 體(32)在選定了合適的毛細材與截面積後，即可 (=)内水位高低的手段來㈣給水流量；毛細材可將^中^ =的^雜質賊，故補水體(32)可兼有第—道過渡功能， (13^^(33)可兼有第二道過濾、功能，在水進人螺^發片 ⑽)則Μ過初步過濾，可增長蒸發片的壽命 ' =33)若太辨’只要取出細更換即可，而不 而將整組螺旋蒸發片（131)拆解。 ' 10.相較於供熱裝置(2)，蒸餾裝置(1)是屬較易耗損的部 ，’傳統供熱裝置與傳統蒸餾裝置，設計上為一整體，傳統擴 散式多效蒸餾系統在維護上較為不便；雖然理論上可以使用各 種，同型式躺、，但傳統的—體式設計’需與整⑽、統配合， 故多是以最方便設計的太陽直接或間接照射的方式，來加熱供 熱褒置，其他的取熱方式則較少見’故蒸餾器的使用範圍受到 限制；故本發明提供將供熱裝置(2)與蒸餾裝置⑴分開而獨立 為單一系統之概念；如此供熱裝置(2)就可以獨立設計製作， 同—套蒸餾裝置(1)還可搭配不同的熱媒(HC) ’應用方式就可 有更多變化。 【實施方式】 以下依據圖面所示的實施例詳細說明如後： 如圖2所示為本發明的立體示意圖，如圖3所示為本發明的 立體分解示意圖，如圖4所示為本發明的橫剖面示意圖，如圖6 所示為本發明的縱剖面示意圖，如圖9所示為本發明實際應用 時的立體裝置示意圖，如圖10所示為為圖9的立體分解示意 201240922 圖，如圖12所示為本發明應用另種支撐結構時的橫剖面示音 圖，如圖13所示為本發明另種實施型態的橫剖面示意圖，= 15所示為本發明另種應祕熱裝置時的橫剖面示意圖，如圖14 所示為本發明另種實施型態的橫剖面示意圖，如圖21所示為本 發明供熱面設有電熱裝置時的橫剖面示意圖。 … 圖式中揭示出，為一種螺旋式多效蒸餾系統，其包括： 一蒸餾系統(100)，該蒸餾系統(100)是由一蒸餾裝置(1)、 一設於該蒸餾裝置(1)中心處的供熱裝置(2)、以及一設於該篆 餾裝置(1)頂端處的補水裝置(3)所組成； 又、只為 其特徵在於： 所述蒸餾裝置(1)是由一片螺旋蒸餾片（1 D所組成； 3亥螺旋洛顧片（11)為呈薄片狀，其一面為供水基氣(H 凝結用的冷凝面(12)，且另-面為作為蒸發用的蒸發面(13); 該蒸發面(13)緊貼有-片以毛細材料所制而成、作為蒸發 用的螺旋蒸發片（131)，並且來自補水裝置⑶之待蒸顧的^ (w) ’能被吸附於該螺旋蒸發片（131)上； 該螺旋蒸館片（11)為從供熱裝置(2)處，以冷凝面(12)、蒸 發面(13)的順序’以一間隔(M)往遠離供熱裝置(2)的方向 螺叙排列設置’且螺旋蒸德片⑼的頂端與底端為呈封閉狀， 以防止水蒸氣(HW)外泄； 在冷嘁面(12)下方，有一供收集由冷凝面(12)滴落之蒗餾 水(DW)用的螺旋集水溝(15); … 藉^供熱裝置(2)提供熱能(p)，讓熱能(p)由螺旋蒸餾片 (η)之最内側圈處的冷凝面(12)處，往外傳導至此冷凝面(12) 相對的洛發面(13)處’再傳導至與此蒸發面(13)緊貼的螺旋蒸 發^(131)上，讓此處螺旋蒸發片（131)所吸附的水(w)，受熱能 (Pk，為水蒸氣(HW)，而此水蒸氣(HW)擴散至位於下一圈處 的冷凝面(12)上時、會凝結成蒸餾水(DW)，此時，水蒸氣(HW) 12 201240922 ϋ為蒸财(DW)的過程中、所放出的潛熱，會往外傳導至 辦目對的蒸發面(13)處，再傳導至與此蒸發面⑽ 的k ΑΧΑ、⑽發片（131)上，又使此處螺旋蒸發片（131)所吸附 的水(W) 1料錢_w)，_，移，娜w)會擴散至 一圈處的冷凝面(12)上、以凝結成蒸鶴水_)，如此重 '直至蒸㈣統_之螺旋蒸鶴片⑼的最外側 圈、^雜熱裝置⑺處，以將熱量排出至蒸館系統_外。 詈m、㈣Ϊ蒸健系統(1〇〇)分為三個部件，分別為：蒸顧裝 在、補水裝置⑶’此模組化之設計將使系統 成太# r祕’紅件損耗後拆賴單，可降低系統維護 用，件即可拆下清洗後重複使 用性將大增 統之使轉命和降低維護成本，系統之實 用ϋ，本發明蒸館系統_幾乎所有體積，都作為基顧 :乎都㈣占的體積很少，蒸餘系統(觸)外部面積， 用，走’散熱面積大增，透與旋蒸賴⑴的使 =多效蒸⑽統，螺纖度=於: 不易.交型，可大大提升熱導率。 者，螺旋蒸鶴片（11)間的間隔(M)，為一由内到外相連 =1、1=^置(2).過多的熱量時，而發生入熱超 結，不像傳統擴散式多效蒸鶴系統，會溢出蒸館片造 連接旋蒸㈣（11)的使用’為—整片從内到外相 系ΐ ’:: 水的均句度佳’不像傳統擴散式多夠 有均勾補水的問題’更讓供熱裝置(2)能以圓柱狀 13 201240922 為外3L易於製作為耐壓的封閉結構，熱源的利用將更有效率。 上述中，所述供熱裝置(2)，為呈柱狀設置，具有一供熱 5(21)，該供熱面(21)的表面，與相鄰螺旋蒸餾片（11)的冷凝面 (=’更覆蓋設有―制大蒸發片(22)，補水裝置同時對此環 狀瘵么片（22)由上方補水，該供熱面(21)能將進入供熱裝置(2) =外，任—型式的能量，轉換成為熱能後、經*供熱面⑼傳 導至，狀蒸發片(22)，使環狀蒸發片(22)上的水蒸發，水蒸汽 擴散凝結於螺旋蒸顧片（11)之最内側圈處的冷凝面(12)上； 而所述環狀蒸發片（22)，其是為下列之一：單獨設置的型 式、和螺旋蒸發片（131)為一體設置的型式。 其中，以此種供熱裝置(2)的設置，讓熱能(P)能順利的由 供熱面(21)處，傳遞至蒸餾裝置(1)上。 b其次，進入供熱裝置(2)的外來任一型式的能量，以蒸氣、 太％能、電能等為主，以方便使用。 再者，透過此環狀蒸發片（22)的設置，讓熱能(P)能順利的 傳出，產生第一次蒸發效果，以於相對冷凝面(12)上，蒸餾出 热鶴水(DW)，並同時避免對冷凝面(12)產生高溫灼傷的傷害， 更能進一步延長供熱裝置(2)的使用壽命。 上述中，所述供熱裝置(2)，是為一流體容器(23)，且流體 容器(23)與供熱面(21)、具有良好的熱接觸、或是同為一體； 而所述流體容器(23)，設有一能供導引任一型式之流體狀 熱媒(HC)、流至供熱面(21)背面、使熱媒(HC)所含之熱能(p)、 能傳導至供熱面(21)、以被蒸餾裝置(1)帶走用的輸入管(24); 以及 * 一能導引前述被取熱後之熱媒(HC)離開的輸出管(25)。 其中，透過此種供熱裝置(2)，降低使用上的困擾，並能 以較低的成本，讓熱能(P)能順利的由供熱面(21)處，傳遞至蒸 餾裝置(1)之處，而且更能使用不同的熱媒(HC)，以配合不同 201240922 的機具[如太陽能加埶機、 用：本發明的泛用性；種:商 置(2㈣電電熱裝 傳送至蒸雕置(1)。“轉換為熱^以透過供熱面⑼ 的難透過此種没置，能讓本發明便於應用，降低應用上 心严上所述供熱裝置(2) ’是由-設於該蒸餾裝置⑴中 ^二冬，顧裂置(1)封閉的定位塞體(26);以及 月t將洛汽輸入洛餾裝置⑴内的蒸汽輸入管(η)所組成。 “中、’透過此種供熱裝置(2)的應用，能降低成本，提高 ，明?運作效果，*且#蒸汽碰到最近的冷凝面⑽後，還 此產生减水(DW) ’達成—雙重蒸躺效果，形成一額外的 補水效果。 上述中’所述補水裝置⑶，具有至少一個裝盛有待蒸德 之水(W)的水槽(31)、及至少—個以毛細材料所製成的補水體 (32)，且該補水體(32)的一端、浸泡於水槽(31)内的水(w)中， 並另一端與螺旋蒸發片（丨31)頂端連接，能將水(W)由水槽(31) 處、引入螺旋蒸發片（131)中； 而所述補水體(32)，其是為下列之一：可單獨拆換的型 式、和螺旋蒸發片（131)為一體設置的型式。 其中，透過此種補水體(32)的設置，能在選定了合適的毛 細材與截面積後，即可以控制水槽(31)内水位高低的手段來控 制給水流量’並可將水中不溶于水的懸浮雜質攔截，兼有第一 道過滤功能。 上述中’所述螺旋蒸餾片（11)，其每一圈之兩側邊緣間， 為呈下列之一的狀態：由内側至外側而緩緩變低、由内側至外 側而皆等高、由内側至外側而缓緩變高。 15 201240922 其次，透過不同的螺旋蒸餾片（11)設置方式，能應對於 同的外型構造設計和蒸餾水、廢水的排出方式，以符^各種^ 商的需要，更讓本發明能應對不同的廠商需求。 敞 上述中，所述蒸餾系統(100)中，更包括一能將蒸餾 έ之餘熱，用以預熱待蒸館之水(W)的熱回收裝置(4); 和輸出端 所述熱回收裝置(4)，是包括至少二第一回熱管(4|) · 又所述第-回熱管⑼的中間段，為設置於螺旋集 (is)内、或與螺旋集水溝⑽内之蒸館水(DW)具有良好的執拉 觸，而第-回熱管⑼的兩端分別為待蒸餾之水(w)之輸= 由輸入端進入第-回熱管(41)的待蒸顧之水(w) :間ΐΓί螺旋集水溝(15)内驗水_内多餘之敎能ί 後，再由輸出端離開傳送至補水裝置(3)。 、、、b(p) 餾之水(w)的熱回收裝置(4); …寺裔 所述熱回收裝置(4)，是包括至少一第二回熱 述第二回熱管(42)的中間段，為設置於螺旋装發片 之輸入端和輸)的兩端，分別為待駿之水W 中間的待蒸館之水(w)，在經過 42)的數量’能依業者的需求，進 本發的設置方式，將 率，且第一、第二4=(0)中’以提昇整體的運作效 16 201240922 行增減。 另外，受到本發明特性的影響，加入熱回收装 量ί會增力”無傳統擴散式多效_統加 入、口收^置⑷’雖可提升效率，但會有使總 另一方面，本發明加入熱回收裝置(4)時，較傳 其續^述螺⑼則（11) ’其頂端與底端的封閉處， 其而斷面為呈_、以供形成-螺旋集水溝(15)用。 用方式’能降低成本，並讓整_度 明能大t f;;=本，在不影響裝置運作的前提下，讓本發 底端ί述Γ所述蒸⑽統(卿)中’更包括—設於外殼體⑶ 置=、讀·轴裝置⑴所產生之廢水(sw则回收農 與底職_⑴)之頂端 再所述支撐結構(14)，用结構(14); 時、其端斷面為呈w r^ 於螺疑蒸館片（11)之底端處 其端斷面為=谢娜㈣端處時、 是螺螺旋蒸卿1)的最外層， 需要—通==^螺=發片_會接觸到外界，因此 裝置⑴，心:響散熱的條件下保護蒸- 17 201240922 其次’受到本發明螺旋構造的影響，不是所有的水都 能蒸餾為蒸餾水(DW) ’還有會有廢水(SW)[如未蒸發的水、含 有雜質的水等]產生，故需要一回收裝置，以回收廢水 (SW)，避免造成環境污染的問題。 再者’本發明蒸德系統(1〇〇)的最大應用，如：海水淡化， 因海水含有大量雜質溶解其中’為了防止雜質結晶於毛細材料 上、使效能降低’必須不斷加入新海水，並將濃縮之廢水排除， 但所排除之廢水含有大量餘熱，將之直接排除相當可惜，而本 發明蒸餾系統(100)所產生蒸餾水(DW)時，亦含有大量餘熱， 若無熱水需求，而將之冷卻散熱、亦是浪費此部份熱量；利用 熱回收裝置(4) ’可將系統中多餘的熱能(p)，透過熱交換的方 式，用以預熱待蒸餾的水(W)，或是用來預熱熱媒(HC)，以提 升運作效率。 上述中，所述第一回熱管(41)，其位於螺旋集水溝(15)之 中間段處，更包覆有一材質為毛細材料、能吸收蒸餾水(DW) 内多餘之熱能(P)用、並與其内第_回熱管(41)做触換、以供 回收熱能(P)用的滞液器(44)。 又上述中，熱回收裝置(4)，更包括一中間段設置於回收 ，置⑹内、以供吸收廢水(sw)内多餘之熱能(p)用的第三回熱 官(43) ’而該第三回熱管(43)的兩端’分別凸出於回收裝置⑹ 的兩側端外，以供輸出/輸入熱媒(HC)用。 凡再上述中’所述第三回熱管(43)，其位於回收裝置(6)之中 間處，亦更包覆有—材質為毛細材料、能吸收廢水(sw)内 多餘之熱能(P)用、並與其内第三回熱管(43)做熱交換、以供回 收熱能(P)用的滯液器(44)。 另上述中’所述第一回熱管(41)處的滯液器(44)，其位於 集水溝(15)最外側圈處的—端，並更料一引水條⑺，該 弓7條⑺的材質為毛細材料，以將進入螺旋集水溝⑽内的蒸 18 201240922 餾水(DW)排出； —而所述引水條⑺處，更設有—對應於刻 瘵餾水(DW)引出於外的水引出裝置(8)。 〃〇、此將 器 Π 其中’第-回熱管(41)位於螺旋集水溝 (44) ’除了用於熱回收之用夕卜，因為位於螺-= 端處的滯液端，更與引水條⑺連接，所以待 能^滯液綱和引水條⑺的毛細力，將^水 _)帶出，能避免產生水滿出或賤出的困擾，—舉兩y館水 其次’因為廢水(SW)N，必定含有多餘的熱能^ 避免浪費，更能透過第三回熱管(43)與滞液器(44)，U 置⑹中廢水(SW)的多餘之熱能_收，降低整體能源的耗損: 再者，透過柯出裝置_應m祕⑽水(㈣ 引出，以ί、使用，能降低蒸館水(DW)被廢水(sw)污染的可能。 另外’被水引出裝置⑻引出的蒸顧水(DW)，受 螺旋構造的影響，多餘的熱能(P)不多，回收價值不大，但欲 再進-步提昇效率’依舊能於此處，增設回熱管[圖中未揭 示]’以回收此處多餘的熱能(P)。 另一方面，被回收的熱能，亦能應用於加熱水(W)及/或是 熱媒(HC)，以提高本發明的能源應用效率。 亡述中，所述補水體(32)，其為可單獨拆換的型式時，與 螺旋蒸發>1 (131)間’更設置有—以毛細材料所製成 器(33)。 处其中，透過水分配器(33)的增設，可兼有第二道過濾功 =，在水進入螺旋蒸發片（131)前經過初步過濾，可增長螺旋 蒸發片（131)的使用壽命。 另一方面，如果補水體(32)和水分配器(33)若太髒，只要 取出清洗或更換即可，而不必像傳統一般，需將整組螺旋蒸發 片（131)拆解。 19 201240922 如圖16所示為本發明設有間隔條時的立體分解示意圖，如 圖17所示為本發明财間隔條_縱剖面實施示意圖，。如_ 所示為本發明财f摘條、並計字聽射㈣的縱剖面實施 不意圖’如圖19所示為本發明設有間隔條、並為弧線型態排列 時的縱剖面實施示賴，如_所示為本發明設·隔條、並 為渦旋型態排列時的縱剖面實施示意圖。 圖中揭示出，上述中，所述蒸餾系統〇〇〇)中，更包括一 平打於螺旋蒸館师)之軸心、垂直設置於螺旋蒸顧片⑼ 内月b將螺方走洛館片（11)處之各間隔(M)分隔、以形成數個區 域(S)的分隔條(9)。 其中’透過分隔條(9)的應用，將各間隔(M)分隔、以形成 數個區域(S)，提高整體的效率。 旦其次’透過區域⑻的設置，能降低熱散逸的機率，讓敎 買的路徑，能更接近直線輻射，以提昇熱效率。 上述中，所述螺旋蒸餾片（11)，是為下列之一：可撓性金 f板^、非可撓性金屬板片、可撓性高奸聚合物板片、非可 撓性南分子聚合物板片。 其中，使用不__螺旋蒸館片⑼，形成不同的應對 ^力、溫度等'級’以符合各種廠商的需要，讓本發明的整體成 本，能應對於不同的廠商需求。 *上述中，所述支稽結構(H)，更能呈下列之一的狀態：一 子形支撐條、梯形支撐條。 其中:透過不_支聽構⑽，以配合螺旋蒸则⑴）， 二」具有③低差或無高低差的螺旋集水溝(15)，以適用於不同 广=姆置⑴’讓本發明的應用範圍更加泛 廠商的t灰。 如®5所不為本發明的橫剖面實施示意圖，如圖7所示為本 兔明的縱實施示意圖’如圖8所示林發明熱能傳輸時的 20 201240922 橫剖面示意圖，如圖η所示為本發明實際應用例的剖面實施示 意圖。 圖式中揭示出，當供熱裝置(2)輪入熱媒(HC)後，熱媒(HC) 的熱能(P) ’為由螺旋蒸顧片（11)的内側圈處，以冷凝面(12)、 蒸發面(13)、間隔(M)的順序，往螺旋蒸顧片（11)的外側圈處、 呈輻射狀傳導。 §熱月b(P)由螺方疋蒸館片（11)之最内側圈處的冷凝面(I])處 時，首先回往外傳導至此冷凝面(12)相對的蒸發面(13)處，再 傳導至與此蒸發面(13)緊貼的螺旋蒸發片（131)上，讓此處螺旋 蒸發片（131)所吸附的水(W)，受熱能(P)蒸發為水蒸氣(HW)， 而此水蒸氣(HW)擴散至位於下一圈處的冷凝面(ι2)上時、會凝 結成蒸餾水(DW)。 9 此時，水蒸氣(HW)凝結為蒸館水(dw)的過程中、所放出 的潛熱[Latentheat]，會往外傳導至此冷凝面(12)相對的蒸發面 (13)處，再傳導至與此蒸發面(13)緊貼的螺旋蒸發片（131)上， 又使此處螺旋蒸發片（131)所吸附的水(w),蒸發為水蒸氣 (HW) ° ..... …… 同樣，水蒸氣(HW)會擴散至位於下一圈處的冷凝面(12) 上、以凝結成蒸餾水(DW) ’如此重複蒸餾過程、直至蒸餾系 統(100)之螺旋蒸傲片（11)的最外側圈、最遠離供熱裝置⑺處， 以將熱量排出至黑館系統(1〇〇)外，同時螺旋蒸發片（131)亦會 將廢水(SW)排出於外。 9 其中，蒸餾水(DW)會藉由引水條(7)與水引出裝置(8)的配 合來排出，而廢水(SW)會透過回收裝置⑹來排出。 其次，最外層的螺旋蒸發片（131)，配合外殼體⑶所產生 的蒸餾水(DW) ’亦能透過殼體集水道(5〗)讓配合水引出裝 ⑻，將蒸餾水(DW)引出。 由此能得知，透過本發明的構造，更模組化、實用化、合 21 201240922 理化’相較于現今的傳統擴散式多效蒸餾系統，能更具產業利 用性、功效性與實用性。 以上，依據圖式所示的實施例詳細說明瞭本發明的構造、 效果’由於符合新穎及進步性要件，遂妥依法提出 惟以上所述僅為本發明之較佳實施例，但本發 修舰，因此舉凡與本發明意旨相符^ 内。文化要在均絲_都應含屬於本創作專利範圍 22 201240922 【圖式簡單說明】 圖2 圖3 圖4 圖5 圖6 圖7 圖8 圖為傳統擴散式多效蒸館系統的原理示意圖 本發明的立體示意圖。 本發明的立體分解示意圖。 本發明的橫剖面示意圖。 本發明的橫剖面實施示意圖。 本發明的縱剖面示意圖。 本發明的縱剖面實施示意圖。 J w j T只口,J田不思_ 〇 圖9 .本發明實際應用時的立體裝置示意圖 ®ΜΩ :么囯ηΛΑ . 本务明熱能傳輸時的橫剖面示意圖 士义又nn由ιμκτ 士 一 圖10 圖11 圖12 圖13 圖14 圖15 圖16 圖17 為圖9的立體分解示意圖 ，一即β干不恩園。 本發明貫際_例的剖面實施示意圖。 ^發明應用另種支撐結構時的橫剖面示意圖。 本發明另種實施型態的橫剖面示意圖。 本發明另種實施型態的橫剖面示意圖。 f發明另種應祕熱裝置_橫剖面示意圖。 發明設有間隔條時的立體分解示意圖。 _· 明設有間隔條時的縱剖面實施示意圖。 實施^圖。W設有間隔條、並為十字賴排列時的縱糾 實施=本發日練_、並输罐姻時的縱剖3Lit is also a source of thermal energy for moisture secrets; the hydration device (3) is a method of obtaining water through the water, and is transported to the steaming scale (1); each component is a separate system and can be dismantled separately. For maintenance, all the capillary components in the butterfly are individually removable. This modular design will make the system easier to assemble, and the components will be dismantled after the component is worn out. The capillary components of the secret towel are the consumables for rapid damage. The right is the design that can be easily replaced by soap. The capillary components can be removed. = Sex = 'Improve the service life of the system and reduce the maintenance of the two systems. 2. Compared with the traditional diffusion. The design of the multi-effect distillation system is much less, the whole steaming age (10)) almost all the volume, used as ^, other unrelated readings, less body, steaming age, system (10)) external area, several 201240922 The heat dissipation area is greatly increased. Through the use of the spiral steamed film (n), the larger the outer layer area is, the higher the heat amount of the outer layer can be increased, so the heat recovery device is added (the latter two are not only efficient) Will increase, traditional diffusion If the steaming system is added to the heat recovery unit (4), the efficiency can be improved, but the total output will be reduced. Compared with the traditional diffusion type multi-effect steaming system, the thickness of the spiral steaming sheet (1) can be thinner. Not easy to change, can greatly improve the thermal conductivity. 3. In the present invention, since the shape of the spiral distillation sheet (u) is such that the curvature of the distillation sheet is large and has a strong structure, the thickness of the vapor deposition sheet can be (4) and the area can be larger. In the traditional diffusion multi-effect steaming (10) system, it has the advantages of easy weight reduction and large size, and only needs to increase the diameter and length. 4. In the present invention, the interval (M) between the spiral distillation sheets (11) is a space which is connected from the inside to the outside. When the heating device (2) inputs excessive heat, it occurs when the heat is overloaded. The steam can be directly spread to the side of the steaming system (1), which has a large heat dissipation area, to listen to the 'transfer of the scatter-type township steaming age system, which will overflow the steamed strips and cause waste. 5. In the present invention, the use of the through-screw distillation sheet (9) is excellent in the self-purification of a whole piece of m-water hydrated from the inside to the outside, unlike the conventional diffusion type multi-effect distillation system, it is difficult to uniformly replenish water. In the present invention, the use of the spiral distillation sheet (11) allows the heating device (2) to be cylindrical, and is easy to be formed into a pressure-resistant closed structure, and is suitable for a closed heat medium circulation system. The use of heat sources will be more efficient. / steaming (10), system (1 (H)) maximum turn, such as: seawater desalination, because seawater contains large impurities dissolved in it, in order to prevent impurities crystallized on the capillary material, so that the performance is reduced, must continue to add new seawater, and will concentrate The waste water is excluded, but the wastewater containing the discharge contains a large amount of waste heat, and it is a pity to directly exclude it; on the other hand, the distilled water (Dw) produced by the present distillation system (1〇〇) also contains a large amount of waste heat, right heat Hot water demand, and cooling it, is also wasting this part of the heat; heat recovery device (4) 'can (4) t excess heat (P), through the heat exchange side 201240922 type, used to preheat the steam Gu's water (w), or used to preheat the heat medium (HC), to improve operational efficiency. 8. In the present invention, through the use of the spiral distillation sheet (11), it is only necessary to set a whole strip back, and the tube is placed in the gully 'through the tube to sneak into the groove _ steaming water for the hot father to change' Recycling the function of steaming waste water; only need to put a whole heat recovery officer under the secret piece, 'replace the waste water through the fluid in the pipe and the waste water discharged from the evaporation piece as a hot father' to recover the waste heat of the waste water; The setting of the thermal return device (4) of the present invention will become simpler and more efficient. ... When the 曰73⁄4丨发片(i3i) is flowing, the flow rate must be moderate. If the flow is more than = take away and reduce the efficiency; the spiral evaporation sheet _ on the: change of the change, usually the heat we use _ : 么太,] is not a sensitive source of heat, at the same time in the key technology that is not sensitive to each part, generally the end of the capillary material into the water outside the barrel, the water in the barrel will be due to capillary force and weight And the sag slowly and continuously from the other end of the output, the cross-sectional area of the capillary material, the horizontal plane and the gross force, is inversely proportional to the distance between the second and the water level and the highest point of the analysis point; The capillary material on the sheet is stretched into the sink directly. The t 2 method is to steam the toilet; the other side is “== the installation time is not enough to make the whole piece of capillary material fail early, more healthy = the beginning of Yang, the invention proposes to use hydration The capillary material, and must be wasted; this thought; on the snail (10) D _ capillary material, made ^ 201240922 The bottom surface of the bottom surface of the spiral evaporation sheet (131) contact bubble into the water (W) in the water tank (31) , the other end and the water distribution body can also be set separately; the water (W) is filled into the water by the hydrating body (32), The body 'spiral evaporation sheet (131) absorbs water from the bottom of the water distribution H (33); the other two are the capillary material, and the top surface of the device (33) is joined as a whole body (32) in which the appropriate capillary material is selected and cut. After the area, the water level can be (=) the water level in the (=) water supply; the capillary material can be ^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^ (33) It can have a second filter and function. When the water enters the human screw (10), the initial filtration can increase the life of the evaporation sheet '=33. If it is too discerning, just remove the fine replacement. Instead, the entire set of spiral evaporation sheets (131) is disassembled. ' 10. Compared with the heating device (2), the distillation unit (1) is a relatively easy-to-deplete part, 'conventional heating unit and conventional distillation unit The design is a whole. The traditional diffusion multi-effect distillation system is inconvenient to maintain. Although it can theoretically use various types and the same type of lying, the traditional-style design needs to cooperate with the whole (10) and so on. Heating or heating is used in the most convenient way to directly or indirectly illuminate the sun. Other methods of heat extraction are less common. The scope of use is limited; therefore, the present invention provides the concept of separating the heating device (2) from the distillation device (1) and independently as a single system; thus the heating device (2) can be independently designed and manufactured, and the same set of distillation device (1) It can also be changed with different heat medium (HC)' application methods. [Embodiment] The following is a detailed description of the following embodiments: Figure 2 is a perspective view of the present invention. 3 is a perspective exploded view of the present invention, and FIG. 4 is a schematic cross-sectional view of the present invention. FIG. 6 is a schematic longitudinal cross-sectional view of the present invention, and FIG. 9 is a practical application of the present invention. FIG. 10 is a schematic exploded view of FIG. 9 and FIG. 12 is a schematic cross-sectional view of the present invention. FIG. 12 is a cross-sectional view of the present invention. FIG. 14 is a cross-sectional view showing another embodiment of the present invention, and FIG. 14 is a cross-sectional view showing another embodiment of the present invention. 21 is shown for the present invention A cross-sectional schematic view of a surface provided with electric heating means. The figure discloses a spiral multi-effect distillation system comprising: a distillation system (100) consisting of a distillation unit (1) and a distillation unit (1) a heating device (2) at the center, and a water replenishing device (3) disposed at the top end of the rectifying device (1); and only characterized by: the distillation device (1) is composed of a piece A spiral distillation piece (1 D consisting of; 3 Helix spiral film (11) is in the form of a sheet, one side of which is a water supply base gas (H condensation surface (12) for condensation, and the other side is evaporation for evaporation) Surface (13); the evaporation surface (13) is closely attached with a sheet made of a capillary material, as a spiral evaporation sheet (131) for evaporation, and ^(w) from the water replenishing device (3) to be steamed. It can be adsorbed on the spiral evaporation sheet (131); the spiral steaming piece (11) is at an interval from the heating device (2) in the order of the condensation surface (12) and the evaporation surface (13) ( M) Threading away from the direction of the heating device (2) and the top and bottom ends of the spiral steaming sheet (9) are closed to prevent water vapor (HW) from leaking; in the cold head (12) under a spiral sump (15) for collecting the condensed water (DW) dripped from the condensing surface (12); ... providing heat energy (p) by means of the heating device (2), allowing the heat energy (p) to be At the condensation surface (12) at the innermost ring of the spiral distillation piece (η), it is conducted outward to the opposite surface (13) of the condensation surface (12) and is re-conducted to be in close contact with the evaporation surface (13). Spiral evaporation ^ (131), let the water (w) adsorbed by the spiral evaporation sheet (131), the heat energy (Pk, is water vapor (HW), and the water vapor (HW) diffuses to the next circle At the condensation surface (12), it will condense into distilled water (DW). At this time, the latent heat released during the process of steam (HW) 12 201240922 蒸 is the steaming (DW) will be transmitted to the office. At the opposite evaporation surface (13), it is conducted to the k ΑΧΑ, (10) hair piece (131) of the evaporation surface (10), and the water (W) adsorbed by the spiral evaporation sheet (131) is fed. w), _, shift, na w) will spread to the condensation surface (12) at one turn, to condense into steamed crane water _), so heavy ~ until the steaming (four) system _ the spiral outer plane (9) of the outermost circle , ^Heat heat device (7), to discharge heat to the steaming system _ outside.詈m, (4) Ϊ steaming system (1〇〇) is divided into three parts, namely: steaming installed in the water supply device (3) 'this modular design will make the system into a too Lai single, can reduce the maintenance of the system, the parts can be removed, the reusability after cleaning will be greatly improved, and the maintenance cost will be reduced. The utility of the system, the steaming system of the invention _ almost all the volume, as the basis Gu: (4) accounted for a small volume, the external area of the steaming system (touch), use, go 'heat dissipation area increased greatly, and the steaming and simmering (1) make = multi-effect steaming (10) system, screw denier = in: not easy The cross-type can greatly improve the thermal conductivity. The spacing (M) between the spiral steaming tablets (11) is one from the inside to the outside = 1, 1 = ^ (2). When too much heat occurs, it enters the thermal super-junction, unlike the traditional diffusion. Multi-effect steaming crane system, will overflow the steaming plate to create a connection with steaming (4) (11) use 'for the whole film from the inside to the outside phase ΐ ':: The uniformity of water is better than the traditional diffusion type enough There is a problem of water replenishment. 'The heating device (2) can be made into a cylindrical shape 13 201240922. The outer 3L is easy to be made into a pressure-resistant closed structure, and the utilization of the heat source will be more efficient. In the above, the heating device (2) is arranged in a column shape, and has a heat supply 5 (21), a surface of the heating surface (21), and a condensation surface of the adjacent spiral distillation sheet (11) ( = 'More coverage with a large evaporation sheet (22), the water supply device at the same time this ring-shaped sheet (22) from the top of the water, the heating surface (21) can enter the heating device (2) = outside The energy of any type is converted into heat energy, and then transmitted to the evaporation sheet (22) via the heating surface (9) to evaporate the water on the annular evaporation sheet (22), and the water vapor diffuses and condenses in the spiral steaming sheet. (11) on the condensation surface (12) at the innermost ring; and the annular evaporation sheet (22), which is one of the following: a separately provided type, and a spiral evaporation sheet (131) are integrally provided In the arrangement of the heating device (2), the heat energy (P) can be smoothly transferred from the heating surface (21) to the distillation device (1). b Next, the heating device is entered ( 2) The energy of any type of external type is mainly based on steam, too much energy, electric energy, etc. In addition, through the setting of the annular evaporation sheet (22), the heat energy (P) can be smoothly transmitted. , the first evaporation effect is generated, so that the hot water (DW) is distilled off on the opposite condensation surface (12), and at the same time, the high temperature burn damage to the condensation surface (12) is avoided, and the heating device can be further extended (2) In the above, the heating device (2) is a fluid container (23), and the fluid container (23) has good thermal contact with the heating surface (21), or is The fluid container (23) is provided with a fluid-like heat medium (HC) capable of guiding any type, flowing to the back surface of the heating surface (21), and heat energy contained in the heat medium (HC) ( p) an input pipe (24) capable of being conducted to the heating surface (21) and carried away by the distillation apparatus (1); and * an output capable of guiding the heat medium (HC) to be taken away from the heat taken The tube (25), wherein the heating device (2) is used to reduce the trouble of use, and the heat energy (P) can be smoothly transferred from the heating surface (21) to the lower cost. Distillation unit (1), and more different heat medium (HC) can be used to match different equipment of 201240922 [such as solar twisting machine, use: generality of the invention; species: commercial (2 (four) electric heating Loading It is sent to the steaming engraving (1). "Converting to heat ^ to pass through the heating surface (9) is difficult to penetrate, which makes the invention easy to apply and reduces the application of the heating device (2)' It is composed of a positioning plug body (26) which is arranged in the distillation device (1), and a steam inlet pipe (?) which is closed in the column (1); "Medium," through the application of this heating device (2), can reduce costs, improve, and improve the operation effect, * and # steam hits the nearest condensation surface (10), which also produces water reduction (DW) ' Achieve - double steaming effect, forming an additional hydrating effect. The above-mentioned 'the water supply device (3) has at least one water tank (31) containing water (W) to be steamed, and at least one water-repellent body (32) made of capillary material, and the water-retaining body ( One end of 32) is immersed in water (w) in the water tank (31), and the other end is connected to the top end of the spiral evaporation sheet (丨31), and water (W) can be introduced into the spiral evaporation sheet from the water tank (31). The water replenishing body (32) is one of the following types: the separately replaceable type and the spiral evaporation sheet (131) are integrally provided. Through the arrangement of the water-retaining body (32), after the appropriate capillary material and the cross-sectional area are selected, the water level in the water tank (31) can be controlled to control the water supply flow rate and the water can be insoluble in water. The suspended impurities are intercepted and have the first filtering function. In the above-mentioned spiral distillation sheet (11), between the two side edges of each turn, it is in a state of one of the following: from the inside to the outside, it gradually becomes lower, from the inside to the outside, and is equal in height, From the inside to the outside, it slowly goes high. 15 201240922 Secondly, through the different spiral distillation sheets (11) setting method, the same external structure design and the discharge method of distilled water and waste water can be used to meet the needs of various manufacturers. Vendor demand. In the above, the distillation system (100) further comprises a heat recovery device (4) capable of preheating the water (W) of the steam to be steamed; and the heat recovery at the output end The device (4) is an intermediate section including at least two first heat recovery tubes (4|) and a first heat recovery tube (9), which is disposed in the spiral set (is) or steamed in the spiral sump (10) The water (DW) has a good pull, and the two ends of the first-return heat pipe (9) are respectively the water to be distilled (w) = the water to be distilled from the input end to the first heat return pipe (41) (w): ΐΓ 螺旋 螺旋 spiral spiral collection ditch (15) inside the water test _ inside the excess 敎 energy ί, then exit from the output to the hydration device (3). , (b) heat recovery device (4) of the distilled water (w); the heat recovery device (4) of the temple is comprised of at least a second heat recovery second heat pipe (42) The middle section, which is set at the input end and the transmission of the spiral loading piece, is the water (w) of the water to be steamed in the middle of the water W in the middle of the water, and the quantity in the 42) can meet the needs of the operator. , the setting method of the local transmission, the rate, and the first and second 4 = (0) in the 'to improve the overall operational efficiency 16 201240922 line increase or decrease. In addition, affected by the characteristics of the present invention, the addition of heat recovery capacity ί will increase the force "no conventional diffusion type multi-effect _ system addition, port collection ^ (4)' can improve efficiency, but there will be a total on the other hand, this When the invention is added to the heat recovery device (4), it is said that the snail (9) is the closed portion of the top end and the bottom end, and the cross section is _, for forming the spiral sump (15). Use the method of 'can reduce the cost, and let the whole _ degree of energy can be large tf;; = this, without affecting the operation of the device, let the bottom of the hair ί Γ Γ 蒸 (10) In addition, the support structure (14) is provided on the top of the outer casing (3), the waste water generated by the read/shaft device (1) (sw is recycled and the bottom _(1)), and the structure (14) is used; The end section is the outermost layer of the wr^ at the bottom end of the snail steaming plate (11), and the end section is = Xie Na (four) end, which is the outermost layer of the spiral spiral steaming 1), need - pass == ^ Snail = hair piece _ will come into contact with the outside world, so the device (1), the heart: protects the steam under the condition of heat dissipation - 17 201240922 Secondly, under the influence of the spiral structure of the present invention, not all water can be distilled into Distilled water (DW) 'There is also wastewater (SW) [such as unvaporized water, water containing impurities, etc.], so a recovery unit is needed to recover waste water (SW) to avoid environmental pollution. 'The largest application of the steaming system (1〇〇) of the present invention, such as: seawater desalination, because seawater contains a large amount of impurities dissolved in 'to prevent impurities from crystallizing on the capillary material, so that the efficiency is reduced', it is necessary to continuously add new seawater, and will concentrate The waste water is excluded, but the excluded waste water contains a large amount of waste heat, and it is a pity to directly exclude it. However, when the distilled water (DW) produced by the distillation system (100) of the present invention also contains a large amount of waste heat, if there is no hot water demand, Cooling and dissipating heat is also wasting part of the heat; using the heat recovery device (4)', the excess heat energy (p) in the system can be used to preheat the water to be distilled (W) by heat exchange, or It is used to preheat the heat medium (HC) to improve the operation efficiency. In the above, the first heat recovery pipe (41) is located at the middle of the spiral water collection ditch (15), and is further covered with a material of capillary material. Can absorb excess water in distilled water (DW) The heat energy (P) is used as a liquid trap (44) for the recovery of thermal energy (P) with the internal heat exchanger (41). In addition, the heat recovery device (4) further includes An intermediate section is disposed in the recovery, disposed in (6) for absorbing the excess heat energy (p) in the waste water (sw) (the third heat recovery officer (43) and the two ends of the third heat recovery pipe (43) respectively Projecting from both sides of the recovery unit (6) for output/input of heat medium (HC). Wherein the third heat recovery tube (43) described above is located in the middle of the recovery unit (6), It is also coated with a stagnation material that is made of capillary material, absorbs excess heat energy (P) in the waste water (sw), and exchanges heat with the third heat recovery pipe (43) for heat recovery (P). Liquid (44). In the above, the liquid trap (44) at the first regenerative tube (41) is located at the end of the outermost circumference of the sump (15), and is more preferably a water guiding strip (7), the strip 7 (7) The material is a capillary material to discharge the steamed 2012042222 distilled water (DW) into the spiral sump (10); and the water guiding strip (7) is further provided with - corresponding to the engraved distilled water (DW) External water extraction device (8). 〃〇, this device Π where the 'first-return heat pipe (41) is located in the spiral sump (44)' except for the heat recovery, because the liquid-staying end at the screw-= end Article (7) is connected, so the capillary force of the liquid stagnation and the water guiding strip (7) can be taken out, and the water _) can be taken out to avoid the trouble of water overflowing or smashing out. SW)N, must contain excess heat energy ^ to avoid waste, more through the third heat pipe (43) and the liquid trap (44), U set (6) waste water (SW) excess heat energy, reduce overall energy Dissipation: In addition, through the espresso device _ should be m secret (10) water ((4), use ί, use, can reduce the possibility of steaming water (DW) contaminated by wastewater (sw). In addition, 'water extraction device (8) Steaming water (DW), affected by the spiral structure, the excess heat energy (P) is not much, the recovery value is not large, but want to further improve the efficiency of 'step can still be here, add a heat recovery tube [not shown in the figure ]' to recover excess heat (P). On the other hand, the recovered heat energy can also be applied to heated water (W) and / or heat medium (HC) to improve the hair Energy application efficiency. In the above description, the hydrating body (32), which is a separately replaceable type, is provided with a capillary material between the spiral evaporation > 1 (131) (made of a capillary material) 33) where the addition of the water distributor (33) can have a second filtration function =, after the water enters the spiral evaporation sheet (131), the initial filtration can increase the service life of the spiral evaporation sheet (131). On the other hand, if the hydrating body (32) and the water dispenser (33) are too dirty, they can be removed for cleaning or replacement, and it is not necessary to disassemble the entire set of spiral evaporation sheets (131) as in the conventional case. 19 201240922 FIG. 16 is a perspective exploded view showing the arrangement of the spacer strip according to the present invention, and FIG. 17 is a schematic view showing the implementation of the financial interval strip according to the present invention. The longitudinal section of the word listening (4) is not intended to be implemented. As shown in FIG. 19, the vertical section of the present invention is provided with spacers and arranged in an arc shape, as shown in FIG. And a schematic diagram of the longitudinal section when the vortex is arranged. The figure reveals that the above , the distillation system 〇〇〇), further includes a shaft centered on the spiral steaming museum), vertically arranged in the spiral steaming film (9), and the interval b will be at the interval of the Luofang Museum (11) (M) Separation strips (9) that are separated to form a plurality of regions (S). Among them, by the application of the separator (9), the intervals (M) are separated to form a plurality of regions (S), thereby improving the overall efficiency. Secondly, through the setting of the area (8), the probability of heat dissipation can be reduced, so that the path of the purchase can be closer to the linear radiation to improve the thermal efficiency. In the above, the spiral distillation sheet (11) is one of the following: a flexible gold plate, a non-flexible metal plate, a flexible high-polymer sheet, and a non-flexible southern molecule. Polymer sheet. Among them, the use of the __ spiral steaming piece (9), forming different 'forces', temperature, etc. 'levels' to meet the needs of various manufacturers, so that the overall cost of the present invention, can meet the needs of different manufacturers. * In the above, the branch structure (H) can be in a state of one of the following: a sub-shaped support strip and a trapezoidal support strip. Wherein: through the non-hearing structure (10), in conjunction with the spiral steaming (1)), and the second spiral gap (15) having a low or no height difference, the invention is applicable to different widths (1) The scope of application is more ubiquitous. For example, the cross-section of the cross-sectional view of the present invention is not shown in FIG. 7. FIG. 7 is a schematic view of the longitudinal implementation of the present invention. FIG. 8 is a schematic cross-sectional view of the 20 201240922 when the invention invents thermal energy transmission, as shown in FIG. A schematic cross-sectional view of a practical application example of the present invention. The figure shows that when the heating device (2) is charged with the heat medium (HC), the heat energy (P) of the heat medium (HC) is the inner ring of the spiral steaming sheet (11) to the condensation surface. (12) The order of the evaporation surface (13) and the interval (M) is radiated in the outer ring of the spiral steaming sheet (11). § When the hot month b(P) is at the condensation surface (I) at the innermost ring of the spiral slab (11), it is first conducted back to the opposite evaporation surface (13) of the condensing surface (12). And then transmitted to the spiral evaporation sheet (131) which is in close contact with the evaporation surface (13), and the water (W) adsorbed by the spiral evaporation sheet (131) is evaporated by the heat energy (P) into water vapor (HW). When this water vapor (HW) diffuses to the condensation surface (ι2) located at the next turn, it condenses into distilled water (DW). 9 At this time, the latent heat (Latentheat) released during the condensation of water vapor (HW) into steaming water (dw) will be conducted to the opposite evaporation surface (13) of the condensation surface (12) and then conducted to The spiral evaporation sheet (131) which is in close contact with the evaporation surface (13) causes the water (w) adsorbed by the spiral evaporation sheet (131) to evaporate into water vapor (HW) ° ..... ... Similarly, water vapor (HW) will diffuse to the condensation surface (12) at the next turn to condense into distilled water (DW) 'This repeats the distillation process until the distillation system (100) spirals the proud film (11) The outermost ring, farthest from the heating device (7), to discharge heat to the outside of the black hall system (1〇〇), while the spiral evaporation plate (131) also discharges the waste water (SW). 9 Among them, distilled water (DW) is discharged by the combination of the water guiding strip (7) and the water take-off device (8), and the waste water (SW) is discharged through the recovery device (6). Next, the outermost spiral evaporation sheet (131), in conjunction with the distilled water (DW) produced by the outer casing (3), can also be taken out through the casing water collecting passage (5) to draw the distilled water (DW). It can be seen that, through the structure of the present invention, it is more modular, practical, and versatile. 2012 20122222 Physicochemicals can be more industrially utilized, functionally and practically compared to the conventional conventional multi-effect distillation system. . In the above, the structure and effect of the present invention have been described in detail according to the embodiments shown in the drawings, and since it is in accordance with the novel and progressive requirements, the above description is only a preferred embodiment of the present invention, but the present invention is The ship, therefore, is consistent with the intent of the present invention. The culture should be in the silk _ _ should be included in the scope of this creation patent 22 201240922 [Simple diagram of the diagram] Figure 2 Figure 3 Figure 4 Figure 5 Figure 6 Figure 7 Figure 8 The schematic diagram of the traditional diffusion multi-effect steaming system A perspective view of the invention. A perspective exploded view of the present invention. A schematic cross-sectional view of the invention. A schematic cross-sectional view of the invention is shown. A schematic longitudinal section of the invention. A schematic diagram of a longitudinal section of the present invention. J wj T only mouth, J Tian does not think _ 〇 Figure 9. Schematic diagram of the three-dimensional device in the practical application of the invention ® Μ Ω : 国 η ΛΑ 本 本 本 本 本 本 本 本 本 本 ι ι ι ι ι ι ι ι ι ι 10 Figure 11 Figure 12 Figure 13 Figure 14 Figure 15 Figure 16 Figure 17 is a three-dimensional exploded view of Figure 9, one is the β dry garden. A cross-sectional view of a cross-sectional example of the present invention. ^Inventive cross-sectional schematic view of the application of another support structure. A schematic cross-sectional view of another embodiment of the invention. A schematic cross-sectional view of another embodiment of the invention. fInvented another kind of heat device _ cross-sectional schematic. The invention is a schematic exploded perspective view of a spacer. _· A schematic diagram of the longitudinal section when the spacer is provided. Implement the ^ map. W is provided with a spacer strip and is arranged for the vertical alignment when the cross is arranged.
實施:意圖本么月°又有叫條、並為·型態排列時的縱剖S 【主要元件=二、面'有電熱裝置時的橫剖面示意圖。 I 蒸餾裝置 II 螺旋蒸餾片 23 201240922 12 冷凝面 13 蒸發面 131 螺旋蒸發片 14 支撐結構 15 螺旋集水溝 2 供熱裝置 21 供熱面 22 環狀蒸發片 23 流體容器 24 輸入管 25 輸出管 26 定位塞體 27 蒸汽輸入管 28 電熱裝置 3 補水裝置 31 水槽 32 補水體 33 水分配器 4 熱回收裝置 41 第一回熱管 42 第二回熱管 43 第三回熱管 44 滯液器 5 外殼體 51 殼體集水道 6 回收裝置 7 引水條 8 水引出裝置 24 201240922 9 分隔條 100 蒸餾系統 W 水 HW 水蒸氣 DW 蒸1留水 SW 廢水 P 熱能 M 間隔 S 區域 HC 熱媒 A 傳統供熱裝置 B 傳統補水裝置 C 傳統蒸餾片 Cl 傳統冷凝面 C2 傳統蒸發面 D 傳統集水溝 25Implementation: Intent of this month, there is a longitudinal section S when it is called a strip and is arranged in a type. [Main components = two, surface] A schematic cross-section of an electric heating device. I Distillation unit II Spiral distillation sheet 23 201240922 12 Condensing surface 13 Evaporating surface 131 Spiral evaporation sheet 14 Support structure 15 Spiral gully 2 Heating unit 21 Heating surface 22 Annular evaporation sheet 23 Fluid container 24 Input tube 25 Output tube 26 Positioning plug body 27 Steam input pipe 28 Electric heating device 3 Water supply device 31 Water tank 32 Water replenishing body 33 Water distributor 4 Heat recovery device 41 First heat recovery pipe 42 Second heat recovery pipe 43 Third heat recovery pipe 44 Liquid trap 5 Outer casing 51 Housing Water collecting channel 6 Recycling device 7 Water guiding strip 8 Water extraction device 24 201240922 9 Separator 100 Distillation system W Water HW Water vapor DW Steam 1 Retained water SW Waste water P Thermal energy interval S Area HC Heat medium A Traditional heating device B Traditional water supply device C Traditional Distillation Sheet Cl Traditional Condensation Surface C2 Traditional Evaporation Surface D Traditional Water Gutter 25