TWI422528B - Solar vacuum desalinator for sea water - Google Patents
Solar vacuum desalinator for sea water Download PDFInfo
- Publication number
- TWI422528B TWI422528B TW099127908A TW99127908A TWI422528B TW I422528 B TWI422528 B TW I422528B TW 099127908 A TW099127908 A TW 099127908A TW 99127908 A TW99127908 A TW 99127908A TW I422528 B TWI422528 B TW I422528B
- Authority
- TW
- Taiwan
- Prior art keywords
- seawater
- layer
- water
- cooling
- solar
- Prior art date
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/138—Water desalination using renewable energy
- Y02A20/142—Solar thermal; Photovoltaics
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/20—Controlling water pollution; Waste water treatment
- Y02A20/208—Off-grid powered water treatment
- Y02A20/212—Solar-powered wastewater sewage treatment, e.g. spray evaporation
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Description
本發明係有關於一種太陽能真空海水淡化器，尤其是指一種利用抽取真空來導入海水，再藉太陽能熱水的溫度來蒸餾海水，使其海水中的水、鹽份分離，達到海水淡化的效果，達到善用資源的環保概念為創新應用者。The invention relates to a solar vacuum seawater desiccator, in particular to a method for extracting seawater by using a vacuum, and then distilling seawater by the temperature of the solar hot water to separate water and salt in the seawater to achieve desalination effect. The concept of environmental protection that makes good use of resources is an innovative application.
按，一般海水淡化裝置係如公告於86年7月21日我國公告第311588號「海水淡化裝置」新型專利案，其裝置係利用船上引擎排氣管及發電機引擎排氣管，配合一冷凝設備所構成，其中該冷凝設備上設有一循環水入水口，一循環水出水口及一蒸餾進水口，而內部設有冷凝管者；其特徵在於：該主引擎排氣管與發電機引擎排氣管的外圍以一金屬板包圍形成一蒸發設備，而且金屬板內部以一隔板區隔該主引擎排氣管及該發電機引擎排氣管，使該主引擎排氣管所在為一密封狀態的蒸汽室，而該發電機引擎排氣管所對應的為一恆溫室；又，蒸汽室上端面開設有進水管及蒸汽管，其中進水管一端延伸進蒸汽室內且對應該主引擎排氣管，另一端連接冷凝設備之蒸餾進水口，而該蒸汽管則與冷凝設備之冷凝管一端相連。According to the general seawater desalination device, it is announced in the new patent case of "Seawater Desalination Device" announced by China's Announcement No. 311588 on July 21, 1986. The device uses the engine exhaust pipe and the generator engine exhaust pipe to cooperate with a condensation. The device comprises a circulating water inlet, a circulating water outlet and a distillation inlet, and a condenser is arranged inside; the main engine exhaust pipe and the generator engine row The periphery of the trachea is surrounded by a metal plate to form an evaporation device, and the inside of the metal plate is separated by a partition plate between the main engine exhaust pipe and the generator engine exhaust pipe, so that the main engine exhaust pipe is sealed. a steam chamber in a state, and the exhaust pipe of the generator engine corresponds to a constant temperature chamber; further, the upper end surface of the steam chamber is provided with an inlet pipe and a steam pipe, wherein one end of the inlet pipe extends into the steam chamber and corresponds to the exhaust of the main engine The other end is connected to the distillation inlet of the condensing device, and the steam pipe is connected to one end of the condensing pipe of the condensing device.
該新型專利案所揭示之蒸汽室以主引擎排氣管熱量將水進行蒸發，其所產生之蒸汽量不高而具有蒸發效率不高之缺點。此外，將進水管一端延伸進蒸汽室內且對應該主引擎排氣管，另一端連接冷凝設備之蒸餾進水口，其大部分蒸汽不會從蒸汽室進入該蒸汽管而產生凝結流回蒸汽室內，因此，其具有無法確實收集蒸餾水之缺點。再者，該裝置進行海水淡化之過程均在常壓下進行。由於常壓下水之沸點為100℃而海水之 沸點與其近似但略高。在該高溫下進行蒸餾時，不僅升溫之耗能增加，於冷凝過程中亦須提供更大之熱交換能力而使冷凝裝置之耗能亦會隨之增加。是以，單位造水量之成本隨之提高。The steam chamber disclosed in the new patent case evaporates water by the heat of the main engine exhaust pipe, and the amount of steam generated is not high and has the disadvantage of low evaporation efficiency. In addition, one end of the inlet pipe extends into the steam chamber and corresponds to the exhaust pipe of the main engine, and the other end is connected to the distillation inlet of the condensing device, and most of the steam does not enter the steam pipe from the steam chamber to cause condensation to flow back into the steam chamber. Therefore, it has a drawback that it is impossible to collect distilled water surely. Furthermore, the process of desalination of the device is carried out under normal pressure. Since the boiling point of water at normal pressure is 100 ° C and seawater The boiling point is similar but slightly higher. When the distillation is carried out at this high temperature, not only the energy consumption for the temperature increase but also the heat exchange capacity during the condensation process is required to increase the energy consumption of the condensing device. Therefore, the cost per unit of water production will increase.
而公告第562917號「蒸汽集中式蒸餾系統」則為針對上述結構常壓下進行蒸餾之缺失，以利用減壓之方式使沸點降低，而使蒸餾之過程能在較低溫下進行，而可以較少之熱能達成液體蒸餾，而利用正常壓狀態，大幅提高效率。Announcement No. 562917 "Steam Centralized Distillation System" is used to reduce the boiling point under the normal pressure of the above structure, so as to lower the boiling point by means of decompression, and the distillation process can be carried out at a lower temperature. Less heat can achieve liquid distillation, and the normal pressure state is used to greatly improve efficiency.
有鑑於此，本發明人秉持多年該相關行業之豐富設計開發及實際製作經驗，針對現有之海水淡化裝置配合蒸汽原理與概念再予以研究改良，以提供一種太陽能真空海水淡化器的設備，來達成海水淡化的設計，以期具有更佳實用價值性之目的者。In view of this, the inventors have been researching and improving the existing seawater desalination equipment with steam principle and concept to provide a solar vacuum desalination device to achieve the rich design and development experience and practical experience of the relevant industry for many years. The desalination design is designed to have a better practical value.
本發明之主要目的即是為提供一種運用天然資源來產生熱能而循環加溫，以利運熱溫來蒸餾海水，使其海水中的水、鹽份分離的海水淡化效果，達到善用資源的環保概念為目的者。The main object of the present invention is to provide a seawater desalination effect by using natural resources to generate heat energy and circulating heating to distill the seawater to separate the water and salt in the seawater, thereby achieving the use of resources. The concept of environmental protection is the purpose.
為達上述目的，本發明提供一種太陽能真空海水淡化器，其特徵與功效如下：其主要係利用抽取真空來導入海水，再藉太陽能熱水的溫度來蒸餾海水，使其海水中的水、鹽份分離，達到海水淡化的效果，其中係設有一基體，於基體內分隔有加熱層、蒸發層及冷卻層，而以太陽能熱水循環設置於加熱層，且藉由穿設加熱層而位於蒸發層的超熱導管，將熱溫傳遞加熱海水，使其海水沸騰的蒸氣接觸冷卻層的超冷導管，而蒸餾形成淡水而收集分段排出，而加熱層之底部則設有排出鹽份的排鹽管；藉此，運 用天然的太陽能資源來進行真空狀的海水淡化，達到善用資源為目的者。In order to achieve the above object, the present invention provides a solar vacuum seawater desiccator, which has the following features and functions: it mainly uses a vacuum to introduce seawater, and then distills seawater by the temperature of solar hot water to make water and salt in the seawater. The separation is carried out to achieve the effect of seawater desalination, wherein a substrate is provided, and a heating layer, an evaporation layer and a cooling layer are separated in the base body, and the solar water is circulated in the heating layer, and is located in the evaporation layer by passing through the heating layer. The superheated pipe of the layer transfers the hot temperature to heat the seawater, and the steam boiling water of the seawater contacts the ultra-cold pipe of the cooling layer, and is distilled to form fresh water and collects and discharges in sections, and the bottom of the heating layer is provided with a row of discharged salt. Salt pipe We use natural solar energy resources to carry out vacuum desalination and achieve the goal of making good use of resources.
本發明一種太陽能真空海水淡化器進一步於基體之加熱層內設有一漏斗狀的環隔板，且由加熱層組設有超熱導管穿過加熱層之環隔板，藉以熱水加熱海水而蒸餾淡化，而於環隔板之底端鹽份沉澱處導接依回收管路，於管路上設有第一、第二隔膜閥，以利用二段式閥門設計，來回收鹽份同時防止外部空氣滲入基體內部，以確保真空狀態者。The solar vacuum seawater desiccator of the present invention further comprises a funnel-shaped annular baffle in the heating layer of the base body, and the heating layer is provided with a superheat pipe passing through the annular baffle of the heating layer, thereby heating the seawater by hot water to be distilled. Desalination, and at the bottom of the ring separator, the salt deposit is guided by the recovery pipeline, and the first and second diaphragm valves are arranged on the pipeline to utilize the two-stage valve design to recover salt while preventing external air. Infiltrated into the interior of the substrate to ensure a vacuum condition.
本發明一種太陽能真空海水淡化器進一步於基體冷卻層內設有冷卻設備，該冷卻設備包含有設於冷卻層之V形冷卻板上的諸多散熱鰭片，且於散熱鰭片上組設有數超冷導管，藉此已將海水蒸發的氣體冷卻凝結水滴而收集者。The solar vacuum desalination device of the present invention further comprises a cooling device in the base cooling layer, the cooling device comprises a plurality of heat dissipating fins disposed on the V-shaped cooling plate of the cooling layer, and the plurality of super cooling elements are arranged on the heat dissipating fins The conduit, whereby the gas that has evaporated from the seawater is cooled and condensed to collect the water droplets.
本發明一種太陽能真空海水淡化器進一步於冷卻板下方設有一承接淡化水的盛槽，該盛槽具有高低設計，以讓水往低處流，再經磁閥開關控制排出，而其係設置有第一段、第二段磁閥開關，以利用二段式開關的設計，來防止外部空氣滲入基體內部，以確保真空狀態者。The solar vacuum desalination device of the invention further comprises a tank for supporting desalinated water under the cooling plate, the tank has a high and low design, so that the water flows to a low place, and then is controlled to be discharged by a magnetic valve switch, and the system is provided with The first and second sections of the magnetic valve switch utilize a two-stage switch design to prevent external air from penetrating into the interior of the substrate to ensure a vacuum condition.
本發明一種太陽能真空海水淡化器進一步設有一保溫儲水桶，該保溫儲水桶係設置出、入循環管來對應太陽能板設備，且利用一動力泵浦將保溫儲水桶內的熱水導入基體之加熱層，再由加熱層設有一導出管連結至保溫儲水桶，以達成太陽能熱水加溫的循環效果。The solar vacuum desalination device of the invention further comprises a heat storage water storage bucket, wherein the heat preservation water storage bucket is arranged to enter and enter the circulation pipe to correspond to the solar panel equipment, and the hot water in the heat preservation water storage bucket is introduced into the heating body by using a power pump. The layer is further provided with a lead-out tube connected to the heat-insulating water storage tank to achieve the circulation effect of the solar water heating.
本發明一種太陽能真空海水淡化器進一步於基體之蒸發層設有一壓力表，壓力表導接一真空抽取設備，以對應將蒸發層的空間抽取形成真空狀態，同時，蒸發層中設有一海水導入管，管壁上具有諸多透孔，以可將海水導入蒸發層，且於海水 導入管上設有一控制閥者。The solar vacuum desalination device of the invention further comprises a pressure gauge on the evaporation layer of the base body, and the pressure gauge is connected to a vacuum extraction device to correspondingly extract the space of the evaporation layer to form a vacuum state, and at the same time, a seawater introduction tube is arranged in the evaporation layer. a plurality of through holes in the wall to introduce seawater into the evaporation layer and in the seawater A control valve is provided on the inlet pipe.
為令本發明之技術手段、發明目的及達成功效有更完整及清楚的揭露，茲於下詳細說明之，並請一併參閱揭示之圖式及元件符號。For a more complete and clear disclosure of the technical means, the object of the invention and the effect of the present invention, the following detailed description, and the accompanying drawings,
首先，請參閱第一~二圖所示，為本發明提供一種太陽能真空海水淡化器整體示意圖，其主要係利用抽取真空來導入海水，再藉太陽能熱水的溫度來蒸餾海水，使其海水中的水、鹽份分離，達到海水淡化，其中包含有：一基體(1)，為由加熱層(11)、蒸發層(12)及冷卻層(13)所構成的主架體，該加熱層(11)中設有一熱容室(111)，而由熱容室(111)內對應設有穿出的複數支超熱導管(112)，且於超熱導管(112)上設有一漏斗狀的環隔板(113)，而於加熱層(11)上方對應設置蒸發層(12)，且蒸發層(12)上方設置冷卻層(13)，於冷卻層(13)底部係設置有一V形冷卻板(131)；一海水導入單元(2)，係對應設置於基體(1)之蒸發層(12)中，主要設有海水導入管(21)，管壁上具有諸多導入海水的透孔(211)，以可將海水導入基體(1)的蒸發層(12)中，而於海水導入管(21)上進一步係設有一入水量的控制閥(22)；一真空抽取設備(3)，係對應導接在基體(1)之蒸發層(12)上，係設有一壓力表(31)對應感測蒸發層(12)內部之真空狀態的壓力；一太陽能熱水循環機構(4)，為對應設置連結於基體(1)之加熱層(11)，其主要設有一保溫儲水桶(41)，該保溫 儲水桶(41)設置有出、入循環管(42)、(43)來對應一太陽能板設備(44)，以將藉由太陽能板設備(44)所產生的熱水循環導入保溫儲水桶(41)內，而該保溫儲水桶(41)連結一動力泵浦(45)，以可將桶內熱水導入基體(1)之加熱層(11)的熱容室(111)內，經由超熱導管(112)傳遞熱能至蒸發層(12)，以將蒸發層(12)中的海水加熱蒸發，續由熱容室(111)設有一導出管(46)連結至保溫儲水桶(41)以循環熱水；一冷卻設備(5)，係對應設置於基體(1)冷卻層(13)之V形冷卻板(131)上，於V形冷卻板(131)上設有諸多散熱鰭片(51)，且於散熱鰭片(51)上組設有數超冷導管(52)，以將低溫傳至V形冷卻板(131)，而讓蒸氣於V形冷卻板(131)凝結成水滴；一淡水收集單元(6)，係對應設置於基體(1)蒸發層(12)內，且對應於冷卻層(13)之冷卻板(131)下方，其係設有一承接淡化水滴的盛槽(61)，該盛槽(61)具有高低設計，以讓水往低處流入管路(62)，於管路(62)上設置有第一段、第二段磁閥開關(63)、(65)，且二磁閥開關間設有一容槽(64)，以承接第一段磁閥開關(63)所導出的淡化水；一鹽份回收單元(7)，其係於蒸發層(12)之漏斗狀的環隔板(113)底端鹽份沉澱處導接一回收管路(71)，於回收管路(71)上設有防止外部空氣滲入第一、第二隔膜閥(72)、(73)者。First, please refer to the first to second figures, the present invention provides a schematic diagram of a solar vacuum desalination device, which mainly uses a vacuum to introduce seawater, and then uses the temperature of the solar hot water to distill the seawater into the seawater. Separating water and salt to achieve seawater desalination, comprising: a substrate (1), which is a main frame composed of a heating layer (11), an evaporation layer (12) and a cooling layer (13), the heating layer (11) is provided with a heat chamber (111), and a plurality of superheated tubes (112) are provided in the heat chamber (111) correspondingly, and a funnel is arranged on the superheat tube (112). a ring spacer (113), and an evaporation layer (12) is disposed above the heating layer (11), and a cooling layer (13) is disposed above the evaporation layer (12), and a V shape is disposed at the bottom of the cooling layer (13). a cooling plate (131); a seawater introduction unit (2) corresponding to the evaporation layer (12) of the base body (1), mainly provided with a seawater introduction pipe (21) having a plurality of through holes for introducing seawater (211), wherein seawater can be introduced into the evaporation layer (12) of the substrate (1), and a water inlet control valve (22) is further disposed on the seawater introduction pipe (21). a vacuum extraction device (3) is connected to the evaporation layer (12) of the substrate (1), and is provided with a pressure gauge (31) corresponding to the pressure of the vacuum state inside the evaporation layer (12); The hot water circulation mechanism (4) is provided with a heating layer (11) connected to the base body (1), and is mainly provided with a heat storage water tank (41), the heat preservation The water storage tank (41) is provided with an outlet pipe (42) and (43) corresponding to a solar panel device (44) for introducing the hot water generated by the solar panel device (44) into the heat storage bucket ( 41), the insulated water storage tank (41) is coupled to a power pump (45) for introducing hot water in the barrel into the heat chamber (111) of the heating layer (11) of the base body (1), via the super The heat pipe (112) transfers heat energy to the evaporation layer (12) to heat and evaporate the seawater in the evaporation layer (12), and continues to be connected to the heat storage water tank (41) by the heat capacity chamber (111). Circulating hot water; a cooling device (5) corresponding to a V-shaped cooling plate (131) disposed on the cooling layer (13) of the base body (1), and a plurality of heat dissipating fins on the V-shaped cooling plate (131) (51), and a plurality of ultra-cold conduits (52) are disposed on the heat dissipation fins (51) to transfer the low temperature to the V-shaped cooling plate (131), and the vapor is condensed into a water droplet on the V-shaped cooling plate (131). a fresh water collecting unit (6) correspondingly disposed in the evaporation layer (12) of the base body (1) and corresponding to the cooling plate (131) of the cooling layer (13), which is provided with a tank for supporting the dripping water droplets (61), the trough (61) has a high and low design to allow water The lower part flows into the pipeline (62), and the first section and the second section of the magnetic valve switches (63) and (65) are arranged on the pipeline (62), and a cavity (64) is arranged between the two magnetic valve switches. Desalination water derived from the first stage magnetic valve switch (63); a salt recovery unit (7) attached to the bottom of the funnel-shaped annular partition (113) of the evaporation layer (12) A recovery line (71) is connected to the recovery line (71) for preventing external air from penetrating into the first and second diaphragm valves (72), (73).
請一併參閱第一~四圖所示，於使用時，首先，該基體(1)內係藉由真空抽取設備(3)來將基體(1)之蒸發層(12) 抽取空氣，以形成真空狀態，同時藉由壓力表對應感測蒸發層(12)之真空狀態的壓力，當蒸發層(12)呈真空負壓的狀態時，其海水導入單元(2)之海水導入管(21)會將海水抽入，經由管壁上的透孔(211)，讓海水由蒸發層(12)注入，而承載於漏斗狀的環隔板(113)上方，其導入海水的入水量則由控制閥(22)來對應控制；爾後，再將太陽能熱水循環機構(4)中的熱水導入基體(1)加熱層(11)的熱容室(111)，即經由太陽能板設備(44)所產生的熱水由出循環管(42)導入保溫儲水桶(41)內，而保溫儲水桶(41)連結一動力泵浦(45)〔係可為抽水幫浦〕，以可將桶內熱水導入基體(1)之加熱層(11)的熱容室(111)，經由超熱導管(112)將熱水的熱能傳遞至蒸發層(12)，以將環隔板(113)上方的海水加熱蒸發，續由熱容室(111)之導出管(46)將退溫的熱水導回保溫儲水桶(41)，再藉入循環管(43)將水導回太陽能板設備(44)加熱，以保持熱水循環；接續，加熱層(11)內的超熱導管(46)藉以太陽能熱水循環機構(4)中的熱水將海水加熱，使其蒸發而留下鹽分，而蒸氣上升至冷卻層(13)時，藉由冷卻設備(5)中的超冷導管(52)將低溫傳達到V形冷卻板(131)，讓蒸氣於V形冷卻板(131)凝結成水滴，而蒸氣的溫度也可藉由散熱鰭片(51)來導出，且同時經由超冷導管(52)冷卻；接續，於V形冷卻板(131)所凝結的淡化水滴，經由淡水收集單元(6)之盛槽(61)來承接，且以盛槽(61)高低設計，讓水往低處流入管路(62)，而此時係打開第一段磁閥開關(63)，而關閉第二段磁閥開關(65)，水則流入容槽(64)內， 當容槽(64)蓄水量滿了，再打開第二段磁閥開關(65)，而關閉第一段磁閥開關(63)，來防止外部空氣滲入基體(1)內部，以確保蒸發層(12)的真空狀態；另外，於加熱層(11)之環隔板(113)底端所沉澱的鹽份，係藉由鹽份回收單元(7)之回收管路(71)來導出，且利用二段式閥門設計，即打開第一隔膜閥(72)時，關閉第二隔膜閥(73)，以讓具有鹽粒的稠狀物導入回收管路(71)，爾後，再打開第二隔膜閥(73)，關閉第一隔膜閥(72)，讓鹽粒的稠狀物排出，藉此，以防止外部空氣滲入基體(1)內部，以確保蒸發層(12)的真空狀態者。Please refer to the first to fourth figures together. In use, first, the substrate (1) is used to evacuate the evaporation layer (12) of the substrate (1) by means of a vacuum extraction device (3). The air is extracted to form a vacuum state, and the pressure of the vacuum state of the evaporation layer (12) is sensed by the pressure gauge. When the evaporation layer (12) is in a vacuum negative state, the seawater is introduced into the seawater of the unit (2). The introduction pipe (21) draws in seawater, and the seawater is injected from the evaporation layer (12) through the through hole (211) in the pipe wall, and is carried over the funnel-shaped annular partition (113), which is introduced into the seawater. The amount of water entering is controlled by the control valve (22); then, the hot water in the solar hot water circulation mechanism (4) is introduced into the heat chamber (111) of the heating layer (11) of the substrate (1), that is, via solar energy. The hot water generated by the plate device (44) is introduced into the insulated water storage tank (41) from the outlet pipe (42), and the heat storage water tank (41) is connected to a power pump (45) (which can be a pumping pump). The heat capacity of the hot water (11) of the base body (1) is introduced into the heat chamber (111) of the heating layer (11), and the heat energy of the hot water is transferred to the evaporation layer (12) via the superheat pipe (112) to separate the ring. The seawater above the plate (113) is heated and evaporated, and the dewatering hot water is continuously guided back to the heat preservation storage bucket (41) by the outlet pipe (46) of the heat capacity chamber (111), and then the water pipe is taken by the circulation pipe (43). Back to solar panels Preparing (44) heating to keep the hot water circulating; continuing, the superheating conduit (46) in the heating layer (11) heats the seawater by the hot water in the solar hot water circulation mechanism (4), causing it to evaporate and leave Salt, and when the vapor rises to the cooling layer (13), the low temperature is transmitted to the V-shaped cooling plate (131) by the ultra-cold conduit (52) in the cooling device (5), and the vapor is allowed to flow to the V-shaped cooling plate (131). Condensed into water droplets, and the temperature of the vapor can also be derived by the fins (51) and simultaneously cooled by the supercooling duct (52); successively, the desalinated water droplets condensed on the V-shaped cooling plate (131), via fresh water The tank (61) of the collecting unit (6) is received, and the tank (61) is designed to let the water flow into the pipeline (62) at a low position, and at this time, the first section of the magnetic valve switch (63) is opened. And closing the second section of the magnetic valve switch (65), the water flows into the pocket (64), When the capacity of the tank (64) is full, the second section of the magnetic valve switch (65) is opened, and the first section of the magnetic valve switch (63) is closed to prevent external air from penetrating into the interior of the base (1) to ensure evaporation. The vacuum state of the layer (12); in addition, the salt precipitated at the bottom end of the ring separator (113) of the heating layer (11) is derived by the recovery line (71) of the salt recovery unit (7). And using the two-stage valve design, that is, when the first diaphragm valve (72) is opened, the second diaphragm valve (73) is closed to allow the thick substance having the salt particles to be introduced into the recovery line (71), and then opened again. The second diaphragm valve (73) closes the first diaphragm valve (72) to discharge the thick salt particles, thereby preventing external air from penetrating into the interior of the base body (1) to ensure the vacuum state of the evaporation layer (12). By.
再者，請一併參閱第五圖所示，本發明中所有之設備的運作，如控制動力泵浦(45)的啟閉、海水導入水量的控制閥(22)、真空抽取設備(3)的啟閉、磁閥開關及隔膜閥的啟閉運作，均藉由一控制單元(8)來控制及供電，而其供電方式可採用太陽能電源供應，或一般市電供應者。Furthermore, please refer to the fifth figure, the operation of all the equipment in the present invention, such as controlling the opening and closing of the power pump (45), the control valve (22) for introducing the amount of seawater, and the vacuum extraction device (3). The opening and closing operations of the opening and closing, the magnetic valve switch and the diaphragm valve are controlled and supplied by a control unit (8), and the power supply mode can be a solar power supply or a general utility supplier.
以上所舉者僅係本發明之部份實施例，並非用以限制本發明，致依本發明之創意精神及特徵，稍加變化修飾而成者，亦應包括在本專利範圍之內。The above is only a part of the embodiments of the present invention, and is not intended to limit the present invention. It is intended to be included in the scope of the present invention.
綜上所述，本發明實施例確能達到所預期之使用功效，又其所揭露之具體構造，不僅未曾見諸於同類產品中，亦未曾公開於申請前，誠已完全符合專利法之規定與要求，爰依法提出發明專利之申請，懇請惠予審查，並賜准專利，則實感德便。In summary, the embodiments of the present invention can achieve the expected use efficiency, and the specific structure disclosed therein has not been seen in similar products, nor has it been disclosed before the application, and has completely complied with the provisions of the Patent Law. And the request, the application for the invention of a patent in accordance with the law, please forgive the review, and grant the patent, it is really sensible.
(1)‧‧‧基體(1) ‧ ‧ base
(11)‧‧‧加熱層(11) ‧‧‧heating layer
(111)‧‧‧熱容室(111)‧‧‧Thermal room
(112)‧‧‧超熱導管(112)‧‧‧Superheated catheter
(113)‧‧‧環隔板(113)‧‧‧ Ring partition
(12)‧‧‧蒸發層(12)‧‧‧Evaporation layer
(13)‧‧‧冷卻層(13) ‧‧‧Cooling layer
(131)‧‧‧冷卻板(131)‧‧‧Cooling plate
(2)‧‧‧海水導入單元(2) ‧‧‧sea water introduction unit
(21)‧‧‧海水導入管(21)‧‧‧Seawater introduction tube
(211)‧‧‧透孔(211)‧‧‧through holes
(22)‧‧‧控制閥(22)‧‧‧Control valve
(3)‧‧‧真空抽取設備(3) ‧‧‧vacuum extraction equipment
(31)‧‧‧壓力表(31)‧‧‧ Pressure gauge
(4)‧‧‧太陽能熱水循環機構(4) ‧‧‧Solar hot water circulation mechanism
(41)‧‧‧保溫儲水桶(41) ‧ ‧ insulated storage bucket
(42)‧‧‧出循環管(42) ‧ ‧ out of the loop
(43)‧‧‧入循環管(43)‧‧‧Into the circulation pipe
(44)‧‧‧太陽能板設備(44)‧‧‧ solar panel equipment
(45)‧‧‧動力泵浦(45) ‧‧‧Power Pump
(46)‧‧‧導出管(46)‧‧‧Extraction tube
(5)‧‧‧冷卻設備(5) ‧‧‧Cooling equipment
(51)‧‧‧散熱鰭片(51)‧‧‧Heat fins
(52)‧‧‧超冷導管(52) ‧‧‧Supercooled catheter
(6)‧‧‧淡水收集單元(6) ‧‧‧ Freshwater collection unit
(61)‧‧‧盛槽(61) ‧‧‧
(62)‧‧‧管路(62) ‧‧‧pipes
(63)‧‧‧第一段磁閥開關(63)‧‧‧The first stage of the magnetic valve switch
(64)‧‧‧容槽(64) ‧‧‧ 容容
(65)‧‧‧第二段磁閥開關(65)‧‧‧Second section magnetic valve switch
(7)‧‧‧鹽份回收單元(7) ‧‧‧Salt recovery unit
(71)‧‧‧回收管路(71)‧‧‧Recycling pipeline
(72)‧‧‧第一隔膜閥(72)‧‧‧First Diaphragm Valve
(73)‧‧‧第二隔膜閥(73)‧‧‧Second diaphragm valve
(8)‧‧‧控制單元(8) ‧‧‧Control unit
第一圖：本發明整體示意圖First Figure: Overall schematic of the present invention
第二圖：本發明動作示意圖Second picture: schematic diagram of the action of the present invention
第三圖：本發明冷卻設備局部放大示意圖Third: a partial enlarged schematic view of the cooling device of the present invention
第四圖：本發明淡水收集單元局部放大示意圖Fourth: a partial enlarged view of the fresh water collecting unit of the present invention
第五圖：本發明控制供電方塊圖Figure 5: The control power supply block diagram of the present invention
(1)‧‧‧基體(1) ‧ ‧ base
(11)‧‧‧加熱層(11) ‧‧‧heating layer
(111)‧‧‧熱容室(111)‧‧‧Thermal room
(112)‧‧‧超熱導管(112)‧‧‧Superheated catheter
(113)‧‧‧環隔板(113)‧‧‧ Ring partition
(12)‧‧‧蒸發層(12)‧‧‧Evaporation layer
(13)‧‧‧冷卻層(13) ‧‧‧Cooling layer
(131)‧‧‧冷卻板(131)‧‧‧Cooling plate
(2)‧‧‧海水導入單元(2) ‧‧‧sea water introduction unit
(21)‧‧‧海水導入管(21)‧‧‧Seawater introduction tube
(211)‧‧‧透孔(211)‧‧‧through holes
(22)‧‧‧控制閥(22)‧‧‧Control valve
(3)‧‧‧真空抽取設備(3) ‧‧‧vacuum extraction equipment
(31)‧‧‧壓力表(31)‧‧‧ Pressure gauge
(4)‧‧‧太陽能熱水循環機構(4) ‧‧‧Solar hot water circulation mechanism
(41)‧‧‧保溫儲水桶(41) ‧ ‧ insulated storage bucket
(42)‧‧‧出循環管(42) ‧ ‧ out of the loop
(43)‧‧‧入循環管(43)‧‧‧Into the circulation pipe
(44)‧‧‧太陽能板設備(44)‧‧‧ solar panel equipment
(45)‧‧‧動力泵浦(45) ‧‧‧Power Pump
(46)‧‧‧導出管(46)‧‧‧Extraction tube
(5)‧‧‧冷卻設備(5) ‧‧‧Cooling equipment
(51)‧‧‧散熱鰭片(51)‧‧‧Heat fins
(52)‧‧‧超冷導管(52) ‧‧‧Supercooled catheter
(6)‧‧‧淡水收集單元(6) ‧‧‧ Freshwater collection unit
(61)‧‧‧盛槽(61) ‧‧‧
(62)‧‧‧管路(62) ‧‧‧pipes
(63)‧‧‧第一段磁閥開關(63)‧‧‧The first stage of the magnetic valve switch
(64)‧‧‧容槽(64) ‧‧‧ 容容
(65)‧‧‧第二段磁閥開關(65)‧‧‧Second section magnetic valve switch
(7)‧‧‧鹽份回收單元(7) ‧‧‧Salt recovery unit
(71)‧‧‧回收管路(71)‧‧‧Recycling pipeline
(72)‧‧‧第一隔膜閥(72)‧‧‧First Diaphragm Valve
(73)‧‧‧第二隔膜閥(73)‧‧‧Second diaphragm valve
Claims (7)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| TW099127908A TWI422528B (en) | 2010-08-20 | 2010-08-20 | Solar vacuum desalinator for sea water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| TW099127908A TWI422528B (en) | 2010-08-20 | 2010-08-20 | Solar vacuum desalinator for sea water |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| TW201208985A TW201208985A (en) | 2012-03-01 |
| TWI422528B true TWI422528B (en) | 2014-01-11 |
Family
ID=46763422
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| TW099127908A TWI422528B (en) | 2010-08-20 | 2010-08-20 | Solar vacuum desalinator for sea water |
Country Status (1)
| Country | Link |
|---|---|
| TW (1) | TWI422528B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI809591B (en) * | 2021-12-08 | 2023-07-21 | 四季洋圃生物機電股份有限公司 | Sea and fresh water separation device |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114538550B (en) * | 2020-11-19 | 2023-11-10 | 山东大学 | Solar sea water desalting device of vacuumizing device |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWM330859U (en) * | 2007-09-29 | 2008-04-21 | Sheng-Shu Lin | Pressure-reducing type solar heating and desalinating apparatus of sea water |
| CN101503227A (en) * | 2008-02-04 | 2009-08-12 | 陈兆松 | Greenhouse distillation purification apparatus and greenhouse distillation purification method |
| TW200936509A (en) * | 2008-02-22 | 2009-09-01 | Noble Advancement Technology Company | Equipment and method of seawater desalination |
| CN101723476A (en) * | 2010-01-28 | 2010-06-09 | 上海交通大学 | Seawater desalination device employing solar energy and vapor compressing distillation |
-
2010
- 2010-08-20 TW TW099127908A patent/TWI422528B/en not_active IP Right Cessation
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWM330859U (en) * | 2007-09-29 | 2008-04-21 | Sheng-Shu Lin | Pressure-reducing type solar heating and desalinating apparatus of sea water |
| CN101503227A (en) * | 2008-02-04 | 2009-08-12 | 陈兆松 | Greenhouse distillation purification apparatus and greenhouse distillation purification method |
| TW200936509A (en) * | 2008-02-22 | 2009-09-01 | Noble Advancement Technology Company | Equipment and method of seawater desalination |
| CN101723476A (en) * | 2010-01-28 | 2010-06-09 | 上海交通大学 | Seawater desalination device employing solar energy and vapor compressing distillation |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI809591B (en) * | 2021-12-08 | 2023-07-21 | 四季洋圃生物機電股份有限公司 | Sea and fresh water separation device |
Also Published As
| Publication number | Publication date |
|---|---|
| TW201208985A (en) | 2012-03-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105565412B (en) | A kind of outer coagulating type tilts core pattern solar distilling seawater desalinating device | |
| CN103908788B (en) | MVR heat pump evaporation system | |
| CN104329826B (en) | The vertical big temperature difference of multistage of a kind of double-barrel structure absorbs machine | |
| CN102225238A (en) | Evaporation concentration system combining vapor compressor and high-temperature heat pump | |
| CN104848284A (en) | Steam condensation water heat recovery method and device | |
| CN102381796A (en) | Solar photovoltaic photothermal integrated device for seawater desalination | |
| CN107029446A (en) | Double caloics couple solution condensing crystallizing system and method | |
| CN105091509A (en) | Vacuum drying device for heat pump | |
| CN102748963B (en) | Closed water cooling system with double-evaporative cooling pressure | |
| TWI422528B (en) | Solar vacuum desalinator for sea water | |
| RU160016U1 (en) | INSTALLATION FOR WATER | |
| CN205527829U (en) | Formula of condensing outward slope core pattern solar energy distillation sea water desalination device | |
| CN109368727A (en) | Energy-efficient low-temperature negative-pressure evaporating waste water processing method and processing system | |
| CN104129804B (en) | A kind of integral type evaporation and crystallization system and technique | |
| CN103251123B (en) | A kind of vacuum conditioner residual neat recovering system | |
| CN206103382U (en) | Rapid condensation mvr sewage treatment plant | |
| CN207210009U (en) | A kind of solar energy bubbling humidifies semiconductor sea water desalinating unit | |
| CN203494188U (en) | Double-effect concentrator | |
| CN102219270B (en) | Multifunctional water distilling machine | |
| CN213739032U (en) | Novel initiative recovery latent heat disk type solar energy sea water desalination device | |
| CN109205720A (en) | Back self-water storage type multi-stage solar still | |
| CN104019591A (en) | Novel ammonia refrigeration oil collector | |
| CN104229913B (en) | A kind of solar water distiller all-in-one | |
| CN104457309B (en) | A kind of tubular condensing heat exchanger and heat-exchange method thereof | |
| CN106017121A (en) | Gradient vacuum-evaporation low-temperature waste heat recovery system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MM4A | Annulment or lapse of patent due to non-payment of fees |