200821266 九、發明說明： 【發明所屬之技術領域】 本發明係關於海水淡化或水淨化設備，尤指一種利 用進水設備引進海水或河川水，作為淡化或淨化用水， 及冷卻設備之冷卻水，再以蒸氣設備之加熱器對設備内 之海水或河川水進行高溫加熱以產生蒸氣，並於加熱過 程加以適當之授拌，使得蒸氣產生過程中隨時加入之海 水或河川水可以快到達產生蒸氣之溫度，並將結晶鹽排 入儲鹽槽直中收集再利用，且蒸氣並以冷卻設備冷卻成 常溫水，利於飲用之海水淡化或水淨化設備。 【先前技術】 按目前海水淡化裝置，如台灣專利申請第 085212405 ··海水淡化裝置，主要是利用船上主引擎排氣 管及發電機引擎排氣管，配合一冷凝設備上設有一循環水 入水口，一循環水出口水及一蒸顧進水口，而内部設有冷 凝管，並在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，並以隔板區隔主引擎排氣 管及該發電機引擎排氣管，使主引擎排氣管所在為一密 封狀態的蒸汽室，蒸汽室上端面開設有進水管及蒸汽管， 進水管一端延伸進蒸氣室内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，而該蒸氣管則與冷凝設 備之冷凝管一端相連。 又如台灣發明專利申請第086106791號：多級透汽蒸 餾之海水淡化法，其係設有透汽室，透汽室内部以疏水 性多孔有機膜及冷卻壁分別隔離成較高溫之海水區、冷 凝區及較低溫之海水區；再者，將高溫海水輸入透汽室 之較高溫海水區，且將低溫海水輸入透汽室之較低溫海 水區’如此’尚溫海水之蒸汽會透過疏水性多孔有機而 200821266 於有低溫海水於旁側流動之冷卻壁上冷凝為水滴，即可 經冷凝區流出淡水；透汽室流出之淡水會分別流入熱交 換器，以便使其冷卻並回收淡水中之熱量，且熱交換器 會依序將淡水匯集至集水槽。 次如台灣發明專利申請第091208644號：海水淡化系 統，包括熱媒循環系統及熱交換淡化系統構成，其中熱 媒循環系統係在集熱器前端連接幫浦及熱媒儲槽，末端 連接熱交換淡水系統之熱交換器，並在該熱交換器另端 由一回流管與幫浦連通，形成一熱媒循環系統；該熱交 換淡化系統，係在熱交換器設進水室、蒸發室、分離室， 蒸發室内裝置複數排管，連通進水室及分離室，該分離 室内裝設一折流板形成阻隔過濾，分離室連接二次分離 室及儲存槽，藉由二次分離室與分離室的阻隔過濾形成 多次分離作用者；在集熱器與熱媒管間連固設傳動輪， 由驅動件帶動轉動，另一侧連通之熱媒流管設溫度感測 器。 再如台灣發明專利申請第092127253號：海水淡化與淨 化之方法與裝置，包括上、中、下層體及外部冷凝體， 外各層體由加熱單元、淡化裂解單元、淨化分顧單元及 冷卻單元等構成；加熱單元透過蒸氣導管將沸騰的水蒸 氣導入淡化裂解單元内對海水做加熱沸騰，並經由淡化 裂解單元與淨化分餾單元的相互重覆循環，透過分離還 原器的多重裂解步驟與分餾器的重覆淨化過程，可以將水 份子内的元素裂解到最細微後再經淨化重組成為最適合 人體飲用之海洋生成水。 另如台灣發明專利申請第092127255號：可直接生飲 之海水淡化與淨化之裝置，係由可分離式上、下層體及 外部冷凝體組成，各層體主要由四個主要單元所構成； 7 200821266 下層體包括加熱單元， _ 熱室、進水口、雜質成八「叹σ一、裔氣加熱器、力 ? , 成分沉澱區、雜質成分;yi：枚 加 2=力:熱器連接於加熱單元底座直接及賡 熱衣置所產生的熱量，加 接收外部加 熱時因迴流的影響而加速;二騰受 1==-旋渦式的旋轉使海水更加快；：力達，器 L !蒸氣上昇至淡化裂解單元内ί:]彿 置ΐ，透:通力器埶置空間則4 =器?巧導引;用===以 包括，淨化分餾單元，内 八 々又愿，上層體 其餘内置空間則為次一尸α又刀田TO，母刀餾器設分氣管， -層分鶴器内部置室’透過數層分館器及每 生的物理導引作：根：氣管與高溫水蒸氣氣壓撞擊所產 效應性的_.夕卜心將脫離水面的水蒸氣更進一步做- 桶，藉由導㈣ 水蒸氣導引至冷凝插t34種種早凡重覆淡化及淨化之 則滴入冷凝桶，而冷卻成水滴的生成水 的材料將冷凝後的也=糸、、先利用活性碳等能脫臭及脫氯 由生成水出水口成水進行一淨化及脫氯的動作，再 結；藉由上、下尽_下設之一或數個集水容器内做一集 熱單元、淡化杂及外部冷凝體的組合’經由内部加 並透過分離還早兀與淨化分餾單元的相互重覆循環， 過程，再重組水ί的多重淡化步驟與分餾器的重覆淨化 (淨水）不需细疒疋素使其成為淨水，使產生之生成水 再又如1^處理便可達到人體飲用之標準。 與發電共生^ 明專，申請第092132545號：海水淡化 運輸液體；其包含幫浦，設置於系統各單元中幫助 月’官路’為系統各單元間液體與氣體之通 8 200821266 道； 凝結器，使用海水作為冷卻水，凝結來自低壓汽輪機之 蒸汽；第一熱交換器，交換海水及來自第二熱交換器之 純水熱能；同步器，接受來自凝結器及第一熱交換器之 海水、锅爐水加熱器之回歸飽和蒸汽、第二熱交換器之 高溫海水，並同時產生海水蒸汽與純水；第二熱交換器， 交換來自同步器之高溫純水及海水之熱能；蒸餾塔，回 流純水以除去同步器產生之海水蒸汽的殘餘鹽分；純水 收集器，收集系統中所產生之純水；濃鹽水收集器，收集 來自同步器之濃鹽水；蒸汽壓縮機，壓縮來自蒸餾塔之 蒸汽；加熱器，加熱來自蒸汽壓縮機之蒸汽；蒸汽渦輪 機，膨脹來自加熱器之蒸汽以帶動第一發電機和蒸汽壓 縮機；第一發電機，由蒸汽渦輪機帶動發電；再熱爐， 加熱來自蒸汽渦輪機之蒸汽；鍋爐水加熱器，利用來自 再熱爐之蒸汽加熱高低壓鍋爐之水及蒸汽；高壓鍋爐， 可貯存鍋爐水以提供高壓蒸汽，並可接受來自第三熱交 換器之水；低壓鍋爐，可貯存鍋爐水以提供低壓蒸汽， 並可接受來自第四熱交換器之水；高壓汽輪機，膨脹來 自高壓鍋爐之高壓蒸汽以帶動第二發電機；第二發電機， 由高壓汽輪機帶動發電；低壓汽輪機，膨脹來自低壓鍋爐 之低壓蒸汽及在高壓汽輪機膨脹後之蒸氣；第三熱交換 器，交換來自加熱器之燃燒氣體及來自凝結器之水的熱 能；第四熱交換器，交換來自加熱器之燃燒氣體及來自 凝結器之水的熱能。 上述習知者之共同缺點為並未考慮到海水或是河川 水甚至污水進行淨化過程中所生之結晶鹽或雜質等容易 附著於蒸氣室之問題，也就是使用一段時間即必須停機 以清除前述之結晶鹽或雜質，造成使用上之不方便。另 200821266 就製水過程中隨時加入之冷水如何迅速到達產生蒸氣之 效果，亦有欠缺。 為此，本發明者，針對前揭習知者之缺點加以研究 改進，乃發明本案。 【發明内容】 本發明之一目的乃在提供一種海水淡化或水淨化設 備，藉以利用佔用地球大部分空間之海洋之海水直接進 行淡化或淨化，造福缺乏淡水之地區與人民。 本發明之另一目的乃是提供一種海水淡化或水淨化 設備，藉以淨化河川水甚至受污染之水，提昇環保效能。 本發明之特點有： 1 ·本發明之海水淡化或水淨化設備，設進水設備 以引進海水或河川水，作為淡化或淨化用水，及冷卻設 備之冷卻水。 2·本發明之海水淡化或水淨化設備，設蒸氣設備， 蒸氣設備設加熱器，以對設備内之海水或河川水進行高 溫加熱產生蒸氣，並於加熱過程加以適當之攪拌，使得 蒸氣產生過程中隨時加入之海水或河川水可以快到達產 生蒸氣之溫度，並將結晶鹽排入儲鹽槽直中收集再利用。 3 ·本發明之海水淡化或水淨化設備，於冷卻設備 之前設抽氣設備’該抽氣設備並設蒸氣抽取機及蒸氣加 壓槽，以方便將蒸氣輸送到冷卻設備，冷卻設備設第一 及第二冷卻室，以將蒸氣冷卻成常溫水，利於飲用。 4 ·本發明之海水淡化或水淨化設備，為使得海水 淡化效果更明確，係以先經過解析去除大部分雜質之水 作為本設備之原水，提昇海水一次之淡化效果。 【實施方式】 如此，為使貴審查員可充份了解本發明，茲依附 10 200821266 圖式解說如下： 備實: = Γ = 進水設備1，進水設備1設有抽水幫浦i 其中抽水幫浦10並可抽取海水或河川 淨化用水，及抽水幫浦1丄並可抽取 次化或 卻設備之冷卻水。 抽取/母水或河川水，冷 瘵氣設備2 ’蒸氣設備2設蒸氣槽2 〇，於 2 0設加熱器’加熱器可以為瓦斯燃燒器2丄第： ，所不）或是重油燃燒機2 1 A (如第三圖所示）了 利用加熱器以對蒸氣槽2Q内之海水或河川水進=、田 ί以產生洛氣’當然若是採用重油燃燒機2 1 A於蒸 ，槽之外表面必須以適當之隔熱材料2 i B區隔之。、& 為使得蒸^產生過程中隨時加人之海水或河川水可以快 到達產生条氣之溫度，乃於蒸氣槽中設有攪拌哭 =拌器2 2包含數擾拌葉2 2 〇 (如第四圖戶;示），擾 ??2並設有複數之貫穿孔2 2 1，利用貫穿孔2 使仔条氣槽2 0中之水得以流動均勻並於加埶 被適當的授拌:即使-邊製造蒸氣，—邊加人海;^或^ 二水，也可以讓剛加入之海水或河川水迅速到達產 氧=溫度，無停機之虞，且保持一定之製水量，再& :茱2 2係由傳動元件2 3傳動之，傳動元件2 3可】 二馬達或是其他元件構成，只要能帶動攪拌葉2 2轉 $適合、。又蒸氣槽2 0之底壁2 0 〇梢成錐狀，其優點 二虽進行海水淡化過程所生之結晶鹽，可以利用攪拌 /茱2 2攪動，避免結晶鹽附著於蒸氣槽之内壁；或是進 Ζίϊ化過程所生之雜質不會附著於蒸氣槽之内壁，保 、条氣槽之容納量，又一方面，則是可使得所生之結晶 11 200821266 鹽或雜質可以被迅速導引入儲槽2 4中儲放收集再利 用。夂者，於蒸氣槽侧並設有水量計2 ^，皮暑外9 R 内設浮球2 5 Q，浮球2 5 0可隨蒸氣槽2 ◦之水量高 度而運作，確保蒸氣槽中之水量被保持一定，避免保持 蒸氣產生量者。又於蒸氣槽内上方設管路2 6，可將高 壓狀態之蒸氣輸送到下-設備中，t然於管路2 6中並 必須設有適當之阻逆閥、調節閥等屬習知技術，在此不 子警械。 产抽氣设備3，抽氣設備3設有前述管路2 6中，抽 氣設^並設蒸氣抽取機3 〇，可以自前述蒸氣設備2 抽取療氣，並輸送到蒸氣加壓槽3 i中，具有集中蒸氣 並產生加壓之效果，再將蒸氣輸送到冷卻設備4中。 冷卻設備4，冷卻設備4設有第一及第二冷卻室4 〇、ί 1 ’第—及第二冷卻室4 Q、4 1均利用前述之 抽水％浦1 1抽取海水或是河川水進行冷卻，冷卻水並 可經由冷卻水出水口 4 2排出，又第一及第二冷卻室4 =、^1内並設環狀管4 〇〇、41〇(如第五圖所示）， 晨狀苔4 0 〇 4 1 0可為環狀圍繞以增加其長度與距 離，更利於I氣被冷卻成水;夜，方便將蒸氣冷卻成^溫 水，並集中於儲水槽4 4中，又淡化或淨化之水，進入 儲水槽4 4儲放之前，並利用一過濾設備4 3過濾之， 該過濾設備4 3係由活性碳、麥飯石等過濾材 供良好之粒狀雜質之過濾效果。 风徒 如此本發明利用蒸氣設備將海水或河川水之基翕 1匕已去除其雜f，並進行淡化或淨化，且充分利用海水 淡化或河川水淨化過程，使得其副產物（鹽）得以被 用或將雜質充分排出，可謂—舉數得，達 設計與效果。 另 < 只用 12 200821266 【圖式簡單說明】 第一圖：本發明運作流程圖。 第一圖·本發明實施例（一）之設備視圖。 f三圖··本發明實施例（二）之設備視圖。 第四圖··本發明之蒸氣槽剖視圖。 苐五圖··本發明冷卻室之剖視圖。 【主要圖號說明】 進水設備1、抽水幫浦1 〇、1 1、 蒸氣設備2、蒸氣槽2 0、瓦斯燃燒器2 1、重、、 燃燒機2 1 A、隔熱材料2 1 B、攪拌器2 2、授摔葉 220、貝牙孔22 1、傳動元件23、儲槽24 量計2 5、浮球2 5 0、管路2 6、 曰 抽氣设備3、療氣抽取機3 0、蒸氣加壓槽3 1 冷卻設備4、第一冷卻室4 0、第二冷卻室4 1、 出水口 4 2、環狀管4 0 0、4 1 〇、過^設備4 3、 儲水槽4 4 13200821266 IX. Description of the invention: [Technical field of the invention] The present invention relates to a desalination or water purification device, and more particularly to a method for introducing seawater or river water by using a water inlet device, as a cooling or purifying water, and cooling water for a cooling device, The seawater or river water in the equipment is heated at a high temperature by a heater of a steam device to generate steam, and is appropriately mixed during the heating process, so that the seawater or river water added at any time during the steam generation process can quickly reach the steam generation. Temperature, and the crystallization salt is discharged into the salt storage tank and collected and reused, and the steam is cooled by the cooling device into normal temperature water, which is favorable for drinking seawater desalination or water purification equipment. [Prior Art] According to the current seawater desalination device, such as Taiwan Patent Application No. 085212405 · Desalination device, mainly using the main engine exhaust pipe and the generator engine exhaust pipe on the ship, and a circulating water inlet is provided on a condensing device. a circulating water outlet water and a steaming inlet, and a condensation pipe inside, and a metal plate surrounded by a main engine exhaust pipe and a generator engine exhaust pipe to form an evaporation device, and a partition plate The main engine exhaust pipe and the generator engine exhaust pipe are arranged such that the main engine exhaust pipe is in a sealed steam chamber, and the upper end of the steam chamber is provided with an inlet pipe and a steam pipe, and one end of the inlet pipe extends into the steam chamber. And corresponding to the exhaust pipe 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 condensation pipe of the condensing device. Another example is the Taiwan Patent Application No. 086106791: a seawater desalination method for multi-stage vapor-exchange distillation, which is provided with a vapor-permeable chamber, and the interior of the vapor-permeable chamber is separated into a relatively high-temperature seawater region by a hydrophobic porous organic membrane and a cooling wall, respectively. The condensing zone and the lower temperature seawater zone; in addition, the high temperature seawater is input into the higher temperature seawater zone of the permeable chamber, and the low temperature seawater is input into the lower temperature seawater zone of the venting chamber. Porous organic and 200821266 condenses into water droplets on the cooling wall with low-temperature seawater flowing on the side, so that fresh water can flow out through the condensation zone; fresh water flowing out of the steam chamber will flow into the heat exchanger separately, so that it can be cooled and recovered in fresh water. Heat, and the heat exchanger will sequentially collect fresh water into the sump. For example, Taiwan Patent Application No. 091208644: seawater desalination system, including a heat medium circulation system and a heat exchange desalination system, wherein the heat medium circulation system is connected to the pump and the heat medium storage tank at the front end of the collector, and the end is connected to the heat exchange. a heat exchanger of the fresh water system, and at the other end of the heat exchanger, is connected to the pump by a return pipe to form a heat medium circulation system; the heat exchange desalination system is disposed in the heat exchanger and the evaporation chamber, a separation chamber, a plurality of tubes in the evaporation chamber, and a water inlet chamber and a separation chamber. The separation chamber is provided with a baffle plate to form a barrier filter, and the separation chamber is connected to the second separation chamber and the storage tank by the secondary separation chamber and the separation chamber. The barrier filtering of the chamber forms a plurality of separations; the transmission wheel is fixed between the collector and the heat medium tube, and is driven by the driving member, and the temperature medium sensor connected to the other side is provided with a temperature sensor. For example, Taiwan Patent Application No. 092127253: Method and apparatus for desalination and purification of seawater, including upper, middle and lower layers and external condensing bodies, external heating layers, desalination cracking units, purification separation units and cooling units, etc. The heating unit is configured to introduce boiled water vapor into the desalination cracking unit through a vapor conduit to heat boil the seawater, and through a repetitive cycle of the desalination cracking unit and the purification fractionation unit, through the multiple cracking step of the separation reducer and the fractionator Repeating the purification process, the elements in the water can be cracked to the finest and then purified and reconstituted to become the most suitable ocean-derived water for human consumption. Another example is the Taiwan invention patent application No. 092127255: a device for direct seawater desalination and purification, consisting of a separable upper and lower layer body and an external condensate, each layer mainly consisting of four main units; 7 200821266 The lower layer includes a heating unit, _ hot chamber, water inlet, and impurities into eight "sighing sigma, gas heater, force?, component precipitation zone, impurity composition; yi: add 2 = force: heat exchanger is connected to the heating unit The heat generated by the base directly and the hot clothes is accelerated by the influence of the backflow when receiving the external heating; the second is subject to the 1==-vortex rotation to accelerate the seawater; the force reaches the device L! Desalination of the cracking unit ί:] Buddha set ΐ, through: the force of the 埶 埶 则 则 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 4 For the second corpse α and Knife TO, the mother knife distillator is equipped with a gas pipe, - the layer is divided into the internal device of the crane' through several layers of the hall and the physical guidance of each life: root: the trachea and the high temperature water vapor pressure impact The effect of the production of _. 卜 心 heart will be out of the water steamed The gas is further made - the barrel, guided by (4) water vapor to the condensation plug t34 various kinds of early re-duce and purification, then drip into the condensation bucket, and the water-forming material cooled into water droplets will be condensed = 糸First, the deodorization and dechlorination of activated carbon can be used to purify and dechlorinate the water from the water outlet, and then re-cure; one or several water collection containers are provided by the upper and lower sides. Make a combination of heat unit, desalination and external condensate 'through the internal addition and through the separation and early re-circulation and purification fractionation unit re-circulation cycle, process, re-reconstitution water ί multiple desalination step and repeater repeat Purification (purified water) does not require fine quince to make it a clean water, so that the produced water can reach the standard of human consumption as well as the treatment. The symbiosis with power generation ^ Ming special, application No. 092132545: desalination Transport liquid; it contains a pump, which is installed in each unit of the system to help the month 'Guo Lu' as the passage of liquid and gas between the units of the system. 8 200821266; Condenser, using sea water as cooling water, condensing steam from the low pressure turbine; First a heat exchanger for exchanging seawater and pure water heat energy from the second heat exchanger; a synchronizer for receiving seawater from the condenser and the first heat exchanger, returning saturated steam of the boiler water heater, and a second heat exchanger High-temperature seawater, which simultaneously produces seawater vapor and pure water; a second heat exchanger that exchanges heat energy from high-temperature pure water and seawater from the synchronizer; a distillation tower that returns pure water to remove residual salt of seawater vapor generated by the synchronizer; a water collector that collects pure water produced in the system; a brine collector that collects concentrated brine from the synchronizer; a vapor compressor that compresses steam from the distillation column; a heater that heats steam from the steam compressor; a steam turbine , expanding the steam from the heater to drive the first generator and the steam compressor; the first generator is driven by the steam turbine; the reheat furnace heating the steam from the steam turbine; the boiler water heater is utilized from the reheat furnace Steam to heat water and steam in high and low pressure boilers; high pressure boilers to store boiler water to provide high pressure steam and acceptable a water of a third heat exchanger; a low pressure boiler capable of storing boiler water to provide low pressure steam and receiving water from a fourth heat exchanger; and a high pressure steam turbine for expanding high pressure steam from the high pressure boiler to drive the second generator; a two-generator driven by a high-pressure steam turbine; a low-pressure steam turbine that expands low-pressure steam from a low-pressure boiler and a vapor that is expanded after the high-pressure steam turbine; and a third heat exchanger that exchanges heat of combustion gas from the heater and water from the condenser a fourth heat exchanger that exchanges heat from the combustion gases of the heater and the water from the condenser. The common shortcoming of the above-mentioned conventionals is that the problem of easy adhesion of the crystal salt or impurities generated in the purification process of seawater or river water or even sewage to the vapor chamber is not considered, that is, the use of a period of time must be stopped to clear the foregoing The crystalline salt or impurities cause inconvenience in use. In addition, 200821266, there is also a lack of how the cold water added at any time during the process of water production can quickly reach the effect of generating steam. To this end, the inventors of the present invention have invented the present invention in view of the shortcomings of the prior art. SUMMARY OF THE INVENTION One object of the present invention is to provide a desalination or water purification device for directly purifying or purifying seawater that occupies most of the earth's oceans, thereby benefiting areas and people lacking fresh water. Another object of the present invention is to provide a desalination or water purification device for purifying river water or even contaminated water and improving environmental performance. The features of the present invention are as follows: 1. The seawater desalination or water purification apparatus of the present invention is provided with water inlet equipment for introducing seawater or river water as a desalinating or purifying water, and cooling water for cooling the equipment. 2. The seawater desalination or water purification device of the present invention, which is provided with a steam device, and a steam device is provided with a heater for heating the seawater or river water in the device to generate steam, and appropriately stirring the heating process to make the steam generation process The seawater or river water added at any time can reach the temperature at which the steam is generated, and the crystal salt is discharged into the salt storage tank and collected for reuse. 3 · The seawater desalination or water purification device of the invention has a pumping device before the cooling device. The pumping device is provided with a steam extracting machine and a steam pressurizing tank to facilitate the delivery of the steam to the cooling device, and the cooling device is first. And a second cooling chamber to cool the steam into normal temperature water for drinking. 4. The seawater desalination or water purification device of the present invention is used to make the seawater desalination effect more clear, and the water which has been analyzed and removed most of the impurities is used as the raw water of the device to enhance the desalination effect of the seawater once. [Embodiment] In this way, in order to enable the examiner to fully understand the present invention, the following explanations are given as follows: 备 : = = Γ = water inlet equipment 1, water inlet equipment 1 is equipped with pumping pump i The pump 10 can also extract seawater or river purification water, and pump the pump 1 丄 and extract the cooling water of the secondary or equipment. Extraction / mother water or river water, cold helium equipment 2 'Vapor equipment 2 set steam tank 2 〇, set the heater at 20 'heater can be gas burner 2 丄:, no) or heavy oil burner 2 1 A (as shown in the third figure), using a heater to enter the seawater or river water in the steam tank 2Q, and to generate the Luo gas. Of course, if the heavy oil burner 2 1 A is used for steaming, the tank The outer surface must be separated by a suitable insulating material 2 i B. , & In order to make the water or river water at any time during the steaming process, the temperature of the gas can be reached quickly, and there is a stirring in the steam tank. The stirrer 2 2 contains the number of mixed leaves 2 2 〇 ( As shown in the fourth figure; showing), the interference 2 is provided with a plurality of through holes 2 2 1. The through hole 2 is used to make the water in the trough gas trough 20 evenly flow and is properly mixed during the twisting. : Even if you make steam, you can add sea water; ^ or ^ two waters, you can let the newly added sea water or river water quickly reach oxygen production = temperature, no downtime, and maintain a certain amount of water, then &; : 2 2 is driven by the transmission element 23, the transmission element 2 3 can be composed of two motors or other components, as long as it can drive the stirring blade 2 2 to $. Further, the bottom wall of the steam tank 20 has a taper shape, and the advantage is that although the crystal salt produced by the seawater desalination process can be stirred by stirring/twisting, the crystal salt is prevented from adhering to the inner wall of the steam tank; The impurities produced by the process of Ζ ϊ 不会 不会 不会 不会 不会 不会 , , , , , 杂质 杂质 杂质 杂质 杂质 杂质 杂质 杂质 杂质 杂质 2008 2008 2008 2008 2008 2008 2008 2008 2008 2008 2008 2008 2008 2008 2008 2008 2008 2008 2008 2008 2008 2008 2008 2008 2008 2008 The storage tanks in the storage tank 24 are collected and reused. In addition, there is a water meter 2 ^ on the steam tank side, and a float ball 2 5 Q in the skin heat outside 9 R. The float ball 250 can operate with the water level of the steam tank 2 to ensure the steam tank. The amount of water is kept constant to avoid the amount of steam generated. Further, a pipeline 2 6 is arranged above the steam tank to transport the high-pressure steam to the lower-equipment, and in the pipeline 26, it is necessary to provide a suitable anti-back valve, regulating valve, etc. There is no police equipment here. The pumping device 3 is provided, and the pumping device 3 is provided with the above-mentioned pipeline 26, and the pumping device is provided with a steam extracting device 3, and the gas can be taken from the steam device 2 and sent to the steam pressurizing tank 3 In i, there is an effect of concentrating the vapor and generating a pressurization, and then the vapor is sent to the cooling device 4. The cooling device 4, the cooling device 4 is provided with first and second cooling chambers 4 〇, ί 1 '- and the second cooling chambers 4 Q, 4 1 are all extracted by sea water or river water using the pumping water 1 1 described above. Cooling, cooling water can be discharged through the cooling water outlet 4 2, and the first and second cooling chambers 4 =, ^1 are provided with annular tubes 4 〇〇, 41 〇 (as shown in the fifth figure), morning Shaped moss 4 0 〇 4 1 0 can be surrounded by a ring to increase its length and distance, which is more conducive to the cooling of the I gas into water; at night, it is convenient to cool the steam into warm water and concentrate in the water storage tank 4 4 The water that has been diluted or purified is filtered before being stored in the water storage tank 44 and filtered by a filtering device 43. The filtering device 43 is a filtering effect of good granular impurities by a filter material such as activated carbon or medical stone. In this invention, the present invention utilizes a steam device to remove the impurities of the seawater or the river water, and to purify or purify it, and fully utilize the seawater desalination or river water purification process, so that the by-product (salt) can be The use of or the full discharge of impurities can be described as a number, to achieve design and effect. Another < only 12 200821266 [Simple description of the diagram] The first figure: the flow chart of the operation of the present invention. The first figure is a view of the device of the embodiment (1) of the present invention. f3Fig. A view of the device of the embodiment (2) of the present invention. Figure 4 is a cross-sectional view of a vapor channel of the present invention. Figure 5 is a cross-sectional view of the cooling chamber of the present invention. [Main picture description] Inlet equipment 1, pumping pump 1 〇, 1 1, steam equipment 2, steam tank 2 0, gas burner 2 1, heavy, burner 2 1 A, insulation material 2 1 B 2, 2, 2, 2 Machine 30, vapor pressure tank 3 1 cooling equipment 4, first cooling chamber 40, second cooling chamber 4 1 , water outlet 4 2, annular tube 4 0 0, 4 1 〇, over equipment 4 3, Water storage tank 4 4 13