TWM330988U - Forced counter-flow type distillation apparatus - Google Patents

Forced counter-flow type distillation apparatus Download PDF

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Publication number
TWM330988U
TWM330988U TW96217217U TW96217217U TWM330988U TW M330988 U TWM330988 U TW M330988U TW 96217217 U TW96217217 U TW 96217217U TW 96217217 U TW96217217 U TW 96217217U TW M330988 U TWM330988 U TW M330988U
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Taiwan
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evaporation chamber
forced convection
water
item
device described
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TW96217217U
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Chinese (zh)
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Chang-Ren Chen
Yuh-Ping Chang
Huan-Ming Chou
Rong-Fang Hong
Atul Sharma
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Queen Win Technology Co Ltd
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Priority to TW96217217U priority Critical patent/TWM330988U/en
Publication of TWM330988U publication Critical patent/TWM330988U/en

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

M330988 八、新型說明: 【新型所屬之技術領域】 本創作係有關強制對流之蒸顧裝置(一),特指於風管 之出口及入口兩者之間設有螺旋管,而蒸氣流動於螺旋管 内%•目離〜作帛’使水分子碰觸風管壁H结於風管,使 -蒸氣中之水分凝結成為液態水滴者。 -【先前技術】 #,f用之太陽能蒸㈣置,是利用太陽光熱能直接 加熱原水,以達到蒸餾之功效。 请參閱第三圖,為-習用太陽能蒸餾裝置整體結構及 原理示意侧視圖,為中華民國公告第「M265377」號一案中 所揭露之習用技術,其中载明:該太陽能蒸顧裝置包含一 底座(A)、一玻璃罩(B)、一蒸發室(c)、一入水口(D)、 一集水器(E)及一出水管(ρ)。 待祭潑之原水由入水口(D)進入蒸發室(c)後接 鲁受來自上方玻璃罩(B)所穿透之太陽光熱能,再加上基發 室(C)之底座⑴塗覆吸熱塗層,使蒸發室⑺内之原 水因熱s蓄積所產生之高溫而蒸發,當蒸發室(c)内部之 蒸發效應持續而達飽和蒸氣壓時,蒸氣即形成液滴凝結於 玻璃罩(B)之内侧,利用液滴自身之重力將該液滴收率至 集水器⑴,由出水管⑴導出即產出蒸顧水。 此習用前案之缺點如下: 1·持續凝結於玻璃罩内側之液滴,會增加陽光之反射 率,減少陽光穿透進入蒸發室,内部熱能降低之結果會導 5 M330988 致吸熱蒸發及蒸氣凝結之效率降低,且無相因應之具體措 失得以改善此一重大缺點。 2·原水之混合液成份内之雜質長期附著於蒸發室底 部’會降低所塗覆吸熱塗層之熱蓄積效果下降,同樣會導 致吸熱蒸發及蒸氣凝結之效率降低,故必須時常拆卸内部 •進行清洗,既耗時又費力。 • 综上所述,前案所提及關於習用之太陽能蒸餾装置, 儘管能夠達成在蒸餾作業上所具備之基本要求,但在使用 時之熱效率保持與使用便利性上皆存在諸多缺點與不足的 情況下’無法發揮提升蒸餾水產量或脫水量之具體效果。 由於習用之太陽能蒸餾裝置,存在上述之缺失與不 足’基於產業進步之未來趨勢前提下,實在有必要提出具 體的改善方案,以符合產業進步之所需,更進一步提供業 界更多的技術性選擇。 【新型内容】 > 本創作係以解決習用太陽能蒸餾裝置在熱效率保持與 使用便利性等方面不足之缺點,以及在實用化技術等方面 文到限制之問題,一方面在達成提升熱效率保持與蒸餾效 率為目的,另一方面在於增加使用上之便利性及應用之範 圍,以達成所應具備蒸餾之基本功能外,並使其兼具提升 蒸鶴水產量或脫水量之具體效果上之要求。 為了達成上述目的及功能,其具體採行的技術手段及 方案包括: 種強制對流之蒸餾裝置(一),係包含有蒸發室、風 6 M330988 管、螺旋管、風扇及集水槽,其中··蒸發室,A-設有出 口及入:之密閉空間’該蒸發室底部設置一個以上之儲水 槽;風管’為—連接於蒸發室之出口及入口之管路,其位 置最低處設有穿孔;螺旋f,係連接於風管且位於蒸發室 :出口及入口兩者之間;風扇,係設置於蒸發室之出口; 二水槽,係設置於風管外部,並包覆風f之穿孔,集水槽 上述之風管為高傳導性材料。 上述之蒸發室之加熱源可為太陽光、電熱ϋ或火源。 上述之蒸發室之頂板可為一透光材料。 上述之蒸發室之底板為—集熱不透光材料。 上述之蒸發室之底部外設置一具凹曲面之太陽光反射 上述之蒸發室之儲水槽為可移動式。 上述之出水管設置有Ν形管。 • 上述之出水管外接儲水桶。 本創作之優點在於: 丨·可廣泛應用於蒸餾水產製、海水淡化及蔬果乾燥等 產業。 ⑨也2·始、閉之蒸餾空間及強制對流之設計,除隔絕與外界 壞境接觸外’亦可加快處理速度,提高蒸館過程之效率。 二氣刀子與水分子比重不同之物理現象,使基氣 二螺,因離心作用,使水分子碰觸風管壁而凝結;風 g之s壁快速形成水滴,可大幅提升«之蒸氣之冷凝效 7 M330988 果,有效提高蒸餾水產量。 【實施方式】 請參閱第一圖,本創作係包含有:蒸發室(1)、風管 (2)、螺旋管(3)、風扇(4)及集水槽(5),其中: 蒸發室(1)’為一設有出口(11)及入口(12)之密 -閉空間,該蒸發室(1 )底部設置一個以上之儲水槽(13), -該儲水槽(13 )如圖中所示,為複數之抽屜式槽體,為獨 立可移動式設計,以便於清洗;另,該蒸發室(1)之頂板 (14)可為一透光材料及底板(15)為一集熱不透光材料, 作用在於使具高熱能之太陽光得以穿透頂板(14),且熱能 ,中於底板(15)。再,蒸發室⑴之加熱源—般可為太 陽光,由蒸發室⑴之頂板(14)進入;另外,也可以藉 室⑴之底部外所設置一具凹曲面(61)之太“ 反射來自蒸發室⑴上方之太陽光將底板 埶口…、’且’除了天然之熱源外、亦可採行其它之加 …方式,如電熱器或火源等,可於 時’料無太陽能可用之缺點日㈣柄㈣作業 口(=)路為:連接於蒸發室⑴之出口⑴)及入 (2)之,路,其位置最低處設有穿孔 (2)為高傳導性材料。 、另風官 螺旋官(3 )’係連接於風管 之出口’且位於瘵發室(1) (11)及入口(12)兩者之間。 ; 風扇(4),係設置於基 對流裝置。 …、(1)之出口(11)之強制 8 M330988 集水槽(5),係設置於風管(2)外部,並包覆風管(2) 之穿孔(21),另,集水槽(5)設有出水管(η),出水管 (51 ) —端設置一 N形管(52 ),並出水管(51 )另一端外 ^ 一儲水桶⑺’而N形管(52)設置之作用在於避免外 部冷空氣進入或内部之熱空氣流出,以有效隔絕蒸發室⑴ /、風g ( 2)所構成之密閉系統與外界環境接觸,增進蒸顧 -效率以提高蒸餚水之產量。 鲁势使用時,藉由連接於出口 U1)及入口 U2)兩者風 s (2)之間之螺旋管(3),利用空氣分子與水分子比重不 同之物理現象,使蒸氣流動於螺旋管(3)内時因離心作用, 使^刀子碰觸風官(2)之管壁後降溫,而凝結於風管(2) 之I壁快速形成水滴’水滴沿著風管(2)之管壁往下流至 【管(2)位置最低處之穿孔(21),經由穿孔(2υ流入 古、=(5)’再由出水管(51)排出者。由於風管⑴為 巧傳^性材料’故吸收蒸氣之熱能藉由外部空氣作散敎, ♦使風管⑺之温度不致升高,有效提高蒸條水政熱 總結整個蒸氣之蒸餾凝結過程如下: 過程1:儲水槽内之混合液或含水物f〔如海水、淡水 3水果等〕受熱後,水分蒸發充滿蒸發室⑴。 將人過t2·強制對流之風扇(4)自蒸發室(1)出口(11) :3水;7之蒸氣抽入風管(2)並流經螺旋管 匕八 ^風管⑴之管壁而凝結於風管⑴之管壁快速^ 過程3 :水滴可快速沿著風管⑺之管壁往下流至風 9 M330988 管(2 )位置表低處之穿孔(21 ) ’經由穿孔(21 )流入集 水槽(5),再由出水管(51 )排出經n形管(52)流至外 部之儲水桶(7)。 過程4 :降溫後之低濕度空氣經由風管(2)由蒸發室 (1 )之入口( 12 )強制回流,即完成一完整之蒸餾凝結過 ,程。 請參閱第二圖,為本創作一實施例圖螺旋管(3 )構造 之局部立體圖,其中,螺旋管(3)之管徑之間留有間隙& •有利於散熱,且螺旋管(3)之溫度低於蒸氣,使蒸氣之冷 凝效果佳,且由於循環之速度快,相對使蒸餾水之產量高 可達成應用於產製蒸餾水、海水淡化及蔬果脫水等產業之 具體功效。 " 【圖式簡單說明】 第一圖:本創作一實施例整體結構及原理示意侧視圖。 第二圖:本創作一實施例圖螺旋管構造之局部立體圖。 鲁第三圖:習用太陽能蒸餾裝置整體結構及原理示意側视圖。 【主要元件符號說明】 (1) 蒸發室 (11) 出〇 (12) 入口 (13) 儲水槽 (14) 頂板 (15) 底板 (2) 風管 (21) 穿孔 (3) 螺旋管 (4) 風扇 (5) 集水槽 (51) 出水管 M330988 (52) N形管 (6) 太陽光反射裝置 (61) 凹曲面 (7) 儲水桶 (A) 底座 (B) 玻璃罩 (C) 蒸發室 (D) 入水口 (E) 集水器 (F) 出水管M330988 VIII. New description: [New technical field] This creation is about the forced convection steaming device (1). Specifically, there is a spiral tube between the outlet and the inlet of the air duct, and the vapor flows in the spiral. The inside of the tube is removed from the tube to make the water molecules touch the wall of the duct H to the duct, so that the water in the vapor condenses into a liquid drip. - [Prior Art] #, f used in solar steaming (four), is the use of solar thermal energy to directly heat the raw water to achieve the effect of distillation. Please refer to the third figure, which is a schematic side view of the overall structure and principle of the conventional solar distillation unit. It is a conventional technology disclosed in the case of the Republic of China Announcement No. M265377, which states that the solar steaming device includes a base. (A), a glass cover (B), an evaporation chamber (c), a water inlet (D), a water collector (E) and an outlet pipe (ρ). The raw water to be sacrificed enters the evaporation chamber (c) from the water inlet (D) and is then exposed to the solar thermal energy penetrated from the upper glass cover (B), and is coated with the base (1) of the base chamber (C). The heat absorbing coating causes the raw water in the evaporation chamber (7) to evaporate due to the high temperature generated by the accumulation of heat s. When the evaporation effect inside the evaporation chamber (c) continues to reach a saturated vapor pressure, the vapor forms a droplet condensed on the glass cover ( On the inner side of B), the droplet is yielded to the sump (1) by the gravity of the droplet itself, and is discharged from the outlet pipe (1) to produce steamed water. The shortcomings of this prior case are as follows: 1. The droplets that continue to condense on the inside of the glass cover will increase the reflectivity of the sunlight, reduce the penetration of sunlight into the evaporation chamber, and the internal heat energy will decrease. 5 M330988 causes heat absorption and vapor condensation. The efficiency is reduced, and no specific response to the problem can improve this major shortcoming. 2. The impurities in the composition of the raw water mixture adhere to the bottom of the evaporation chamber for a long time, which will reduce the heat accumulation effect of the coated heat absorbing coating, which will also cause the efficiency of heat absorption evaporation and vapor condensation to decrease, so it is necessary to disassemble the interior from time to time. Cleaning is time consuming and labor intensive. • In summary, the solar distillation unit mentioned in the previous case, although it can achieve the basic requirements for distillation work, has many shortcomings and disadvantages in terms of thermal efficiency and ease of use. In the case, 'the specific effect of increasing the production or dehydration of distilled water is not available. Due to the above-mentioned shortcomings and shortcomings based on the future of solar energy distillation equipment, it is necessary to propose specific improvement plans to meet the needs of industrial progress and further provide more technical choices in the industry. . [New content] > This creation is to solve the shortcomings of the conventional solar energy distillation device in terms of thermal efficiency maintenance and ease of use, as well as the limitations of practical technology and other aspects. On the one hand, it achieves the improvement of thermal efficiency and distillation. For the purpose of efficiency, on the other hand, it is to increase the convenience of use and the scope of application, in order to achieve the basic functions of distillation, and to meet the specific effects of increasing the yield or dewatering of steamed crane water. In order to achieve the above purposes and functions, the specific technical means and solutions adopted include: a forced convection distillation device (1), which includes an evaporation chamber, a wind 6 M330988 tube, a spiral tube, a fan and a sump, wherein Evaporation chamber, A- with outlet and inlet: the confined space 'more than one storage tank at the bottom of the evaporation chamber; the air duct' is a pipeline connected to the outlet and inlet of the evaporation chamber, with the lowest position at the bottom The spiral f is connected to the air duct and is located between the evaporation chamber: the outlet and the inlet; the fan is disposed at the outlet of the evaporation chamber; and the second water tank is disposed outside the air duct and covers the perforation of the wind f. The above-mentioned duct of the water collecting tank is a highly conductive material. The heating source of the evaporation chamber described above may be sunlight, electric enthalpy or fire source. The top plate of the evaporation chamber described above may be a light transmissive material. The bottom plate of the evaporation chamber is a heat collecting opaque material. A concave curved surface is disposed outside the bottom of the evaporation chamber to reflect the water storage tank of the evaporation chamber. The above-mentioned outlet pipe is provided with a stirrup pipe. • The water outlet pipe above is connected to the water tank. The advantages of this creation are: 丨· can be widely used in industries such as distilled water production, seawater desalination and vegetable and fruit drying. 9 also 2·Starting and closing distillation space and forced convection design, in addition to isolation and external environment contact, can also speed up the processing and improve the efficiency of the steaming process. The physical phenomenon of the difference between the two gas knives and the water molecules makes the base gas two snails, because of the centrifugal action, the water molecules collide with the air duct wall to condense; the wind g s wall rapidly forms water droplets, which can greatly enhance the condensation of the vapor Effect 7 M330988 fruit, effectively increase distilled water production. [Embodiment] Please refer to the first figure. The creation includes: an evaporation chamber (1), a duct (2), a spiral tube (3), a fan (4), and a sump (5), wherein: an evaporation chamber ( 1) 'As a dense-closed space with an outlet (11) and an inlet (12), more than one storage tank (13) is arranged at the bottom of the evaporation chamber (1), the storage tank (13) is as shown in the figure Shown as a plurality of drawer type tanks, which are independently movable and designed for cleaning; in addition, the top plate (14) of the evaporation chamber (1) can be a light-transmitting material and the bottom plate (15) is a heat collection. The light-transmitting material serves to allow the high-energy sunlight to penetrate the top plate (14), and the heat energy is in the bottom plate (15). Further, the heating source of the evaporation chamber (1) is generally sunlight, which is entered by the top plate (14) of the evaporation chamber (1); in addition, a concave curved surface (61) may be disposed outside the bottom of the chamber (1). The sunlight above the evaporation chamber (1) will smash the bottom plate..., 'and' in addition to the natural heat source, other methods such as electric heaters or fire sources can be used, and the solar energy can be used. Day (4) Handle (4) Working port (=) Road is: connected to the outlet (1) of the evaporation chamber (1) and into (2), the road is provided with a perforation (2) at the lowest position as a highly conductive material. The screw officer (3)' is connected to the outlet of the duct and is located between the burst chamber (1) (11) and the inlet (12). The fan (4) is disposed in the base convection device. (1) The forcing of the exit (11) 8 M330988 The sump (5) is placed outside the duct (2) and covers the perforation (21) of the duct (2), and the sump (5) There is an outlet pipe (η), an outlet pipe (51) is provided with an N-shaped pipe (52), and the other end of the outlet pipe (51) is provided with a water storage tank (7)' and the N-shaped pipe (52) is provided. The function is to prevent external cold air from entering or internal hot air flowing out, so as to effectively isolate the closed system formed by the evaporation chamber (1) /, wind g ( 2) from contact with the external environment, and improve the steam-efficiency to increase the yield of steamed water. When using Lu Shi, the spiral tube (3) between the wind s (2) connected to the outlet U1) and the inlet U2) uses a physical phenomenon in which the specific gravity of the air molecules and the water molecules are different, so that the vapor flows to the spiral. During the tube (3), due to the centrifugal action, the ^ knife touches the wall of the wind commander (2) and then cools, and the wall of the air duct (2) condenses rapidly to form a water droplet 'water droplets along the air duct (2) The pipe wall flows down to the perforation (21) at the lowest position of the pipe (2), and is discharged through the perforation (2υ into the ancient, =(5)' and then discharged from the outlet pipe (51). Since the duct (1) is a good transmission The material 'the heat of absorbing vapor is dissipated by the outside air, ♦ the temperature of the air duct (7) is not increased, and the steaming water heat is effectively increased. The distillation process of the whole steam is as follows: Process 1: Mixing in the water storage tank After the liquid or hydrate f (such as sea water, fresh water, 3 fruits, etc.) is heated, the water is steamed. Fill the evaporation chamber (1). Pass the person t2·forced convection fan (4) from the evaporation chamber (1) outlet (11): 3 water; 7 steam is drawn into the air duct (2) and flows through the spiral tube The wall of the tube (1) condenses on the wall of the duct (1). Process 3: Water droplets can quickly flow down the wall of the duct (7) to the wind. 9 M330988 Tube (2) Perforation at the lower part of the position table (21) ' Flowing through the perforation (21) into the sump (5), and then discharging from the outlet pipe (51) to the external storage tank (7) through the n-shaped pipe (52). Process 4: The low-humidity air after cooling is passed through the air duct ( 2) Forced reflux from the inlet (12) of the evaporation chamber (1) to complete a complete distillation condensation process. Please refer to the second figure, which is a partial perspective view of the structure of the spiral tube (3) according to an embodiment of the present invention, in which a gap is left between the diameters of the spiral tube (3), and the spiral tube is provided. The temperature is lower than the vapor, so that the condensation effect of the vapor is good, and the speed of the circulation is fast, and the specific output of the distilled water is relatively high, so that the specific effects of the industries such as production of distilled water, seawater desalination, and dehydration of fruits and vegetables can be achieved. " [Simple Description of the Drawings] The first figure: a schematic side view of the overall structure and principle of an embodiment of the present creation. The second figure: a partial perspective view of the spiral tube structure of an embodiment of the present invention. Lu 3: A schematic side view of the overall structure and principle of a conventional solar distillation unit. [Explanation of main components] (1) Evaporation chamber (11) Outlet (12) Inlet (13) Water storage tank (14) Top plate (15) Base plate (2) Duct (21) Perforation (3) Spiral tube (4) Fan (5) Sink (51) Outlet M330988 (52) N-tube (6) Solar reflector (61) Concave curved surface (7) Water tank (A) Base (B) Glass cover (C) Evaporation chamber ( D) Inlet (E) Water collector (F) Outlet

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Claims (1)

M330988 九、申請專利範圍: 流之蒸館裝置(一),係包含有: 底邻:、ί至广設有出口及入口之密閉空間,該蒸發室 底邛,又置一個以上之儲水槽; .置最:設有 =接於蒸發室之出一之管路,其位 .者之=旋管’係連接於風管且位於蒸發室之出口及入口兩 風扇,係設置於蒸發室之出口; 切③Γ水, =中請專利範圍第η所述之強制對流之蒸顧裝置 )/、中,風管為高傳導性材料。 (〜),Α申明專利範圍第1項所述之強制對流之蒸餾裝置 該蒸發至之加熱源為太陽光、電熱器或火源。 (,並申明專利範圍第1項所述之強制對流之蒸餾裝置 八,該蒸發室之頂板為一透光材料。 ( 申w月專利範圍第1項所述之強制對流之蒸館裝置 ’,、中’該蒸發室之底板為—集熱不透光之材料。 (1 圍第1項所述之強制對流之蒸顧裝置 反射裝置蒸發室之底部外設置—具凹曲面之太陽光 (〜),a/°月專利範圍第1項所述之強制對流之蒸顧裝置 ,、中,該蒸發室之儲水槽為可移動式。 12 M330988 8、 如申請專利範圍第1項所述之強制對流之蒸餾裝置 (一),其中,該出水管設置有N形管。 9、 如申請專利範圍第1項所述之強制對流之蒸餾裝置 (一),其中出水管外接儲水桶。M330988 Nine, the scope of application for patents: The steaming hall device (1) of the flow includes: the bottom neighbor: ί至广 has a closed space for the exit and the entrance, and the bottom of the evaporation chamber is provided with more than one water storage tank; . Set the most: there is a line connected to the evaporation chamber, the position of the = the coil ' is connected to the duct and is located at the exit of the evaporation chamber and the entrance of the two fans, is set at the exit of the evaporation chamber ; cut 3 Γ water, = the forced convection steaming device described in the η patent range) /, medium, the duct is a highly conductive material. (~), 强制 Declare the forced convection distillation device described in the first paragraph of the patent scope. The heating source to be evaporated is sunlight, electric heater or fire source. (After declaring the forced convection distillation device described in item 1 of the patent scope, the top plate of the evaporation chamber is a light transmissive material. (The forced convection steaming device described in item 1 of the patent scope of the patent application, The bottom plate of the evaporation chamber is a material that collects heat and is opaque. (1. The forced convection steaming device described in Item 1 is provided outside the bottom of the evaporation chamber of the evaporation device. ), the forced convection steaming device described in item 1 of the a/° month patent range, wherein the water storage tank of the evaporation chamber is movable. 12 M330988 8. Forcing as described in item 1 of the patent application scope The convection distillation device (1), wherein the outlet pipe is provided with an N-shaped pipe. 9. The forced convection distillation device (1) according to claim 1, wherein the outlet pipe is externally connected to the water storage tank. 1313
TW96217217U 2007-10-15 2007-10-15 Forced counter-flow type distillation apparatus TWM330988U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
TW96217217U TWM330988U (en) 2007-10-15 2007-10-15 Forced counter-flow type distillation apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW96217217U TWM330988U (en) 2007-10-15 2007-10-15 Forced counter-flow type distillation apparatus

Publications (1)

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TWM330988U true TWM330988U (en) 2008-04-21

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TW96217217U TWM330988U (en) 2007-10-15 2007-10-15 Forced counter-flow type distillation apparatus

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107098420A (en) * 2017-06-08 2017-08-29 浙江大学 Gas-liquid convection type water salt separator
CN107228586A (en) * 2017-07-31 2017-10-03 广东工业大学 One kind collection Water Heat Pipes

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107098420A (en) * 2017-06-08 2017-08-29 浙江大学 Gas-liquid convection type water salt separator
CN107098420B (en) * 2017-06-08 2022-11-11 浙江大学 Gas-liquid convection type water-salt separation device
CN107228586A (en) * 2017-07-31 2017-10-03 广东工业大学 One kind collection Water Heat Pipes

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