TWI842017B - Mass production system of deep sea water desalination for people's livelihood - Google Patents
Mass production system of deep sea water desalination for people's livelihood Download PDFInfo
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本發明深層海水淡化民生用水大量生產系統,係應用高壓重力沉澱池快速沉澱排除深層海水的重金屬、硬度雜質、化學殘留物質等對人體和動植物的有毒物質;再應用冷凍法分離〝鹽、水〞;使生產出來的〝淡水〞和〝鹵水〞,能夠去除有毒物質,保存深層海水營養豐富肥沃的礦物質與微量元素,做為民生用水、農業用水和工業用水使用。 The deep seawater desalination system of this invention is to use high-pressure gravity sedimentation tanks to quickly precipitate and remove heavy metals, hardness impurities, chemical residues and other toxic substances to the human body, animals and plants in deep seawater; then use freezing method to separate "salt and water"; so that the produced "fresh water" and "brine" can remove toxic substances and preserve the nutrient-rich minerals and trace elements in deep seawater for use as water for people's livelihood, agriculture and industry.
〝海冰生成時會將飽和的鹽分析出〞:海水結冰,其實只是淡水結冰,而將鹽分排擠出來,部分來不及流走的鹽分以〝鹵汁〞的狀態被包裹在冰晶之間的空隙裡形成“鹽泡”。此外,還有來不及溢出的氣體被包裹在冰晶之間的空隙裡形成“氣泡”。因此,〝海冰〞實際上是〝淡水冰晶〞、〝鹽泡〞和〝氣泡〞的混合物。 "When sea ice is formed, saturated salt is extracted": When seawater freezes, it is actually fresh water freezing, which squeezes out the salt. Some of the salt that does not have time to flow away is wrapped in the gaps between ice crystals in the form of "halite" to form "salt bubbles". In addition, the gas that does not have time to overflow is wrapped in the gaps between ice crystals to form "air bubbles". Therefore, "sea ice" is actually a mixture of "fresh water ice crystals", "salt bubbles" and "air bubbles".
〝海冰的形成〞:普通的純淨水在4℃時密度達到最大,0℃時為冰點開始結冰。而海水由於含有鹽分,所以密度最大時的溫度Imax和結冰時的溫度I,都與純水不同,而是取決於海水的鹽度。當海水的鹽度不超過千分之24.69時,Imax>I,也就是,表層海水的氣溫逐漸下降時,表層海水的溫度首先達到密度最大的溫度Imax,於是表層海水下沉,下層海水 上浮,形成對流。當氣溫繼續下降接近冰點I,表層海水已經不會往下沉,因為下面的海水密度更大,於是表層海水直接結冰;如果鹽度超過千分之24.69時,Imax<I,此時,表層海水的溫度下降時首先接近冰點I,這時表層海水由於降溫的時候密度變大,所以下沉,而較為溫暖的下層海水因為密度較小而上浮,形成對流,一直到海水結冰為止;這種海水結冰的方式,因為過程來回多次而較緩慢。 "Formation of sea ice": Ordinary pure water reaches its maximum density at 4℃, and begins to freeze at 0℃, which is the freezing point. However, because seawater contains salt, the temperature Imax when the density is the highest and the temperature I when it freezes are different from those of pure water, but depend on the salinity of seawater. When the salinity of seawater does not exceed 24.69 parts per thousand, Imax>I, that is, when the temperature of the surface seawater gradually decreases, the temperature of the surface seawater first reaches the temperature Imax with the highest density, so the surface seawater sinks and the lower seawater floats, forming convection. When the temperature continues to drop and approaches the freezing point I, the surface seawater will no longer sink, because the density of the seawater below is greater, so the surface seawater freezes directly; if the salinity exceeds 24.69 parts per thousand, Imax<I, at this time, the surface seawater first approaches the freezing point I when the temperature drops. At this time, the surface seawater sinks because its density increases when it cools down, while the warmer lower seawater floats up because of its lower density, forming convection until the seawater freezes; this way of seawater freezing is slow because the process goes back and forth many times.
〝水結成冰後,體積增加9%〞:冰的水分子是由氫氧鏈結合而成,其-O-H-O-原子排列在一直線上,由於這個規則性的排列關係,冰的水分子間形成許多的空隙;而沒有氫鏈結合的水分子,就沒有這種規則性的排列,它會盡量的緊密堆積在一起(close packing)。如室溫的水,其氫鏈結合率約為50%,而冰為100%(氫鏈結合比率越高的水,分子間的空隙就越多),也就是,冰較水規則性的排列高,所以冰的分子間空隙大,因此水和冰的重量相同時,冰的體積大9%;而海水乃是鹽分子和水分子,以混合物的狀態相結合,也就是,以物理狀態結合,其結構非常脆弱;而水是由氫、氧兩種元素組成,氫原子質量為1.00794u,是宇宙最輕的元素,氧原子質量為15.9994,僅次於氫和氦,佔第三位,水的原子質量為17.00734;而鹽,氯化鈉NaCl,是由氯、鈉兩種元素組成,氯原子質量為35.45,鈉原子質量為22.9898,鹽的原子質量為58.4398,鹽的密度為2.165;倘若海水慢速結冰,水分子的原子氫氧鏈已規則性的排列在一直線上,水分子間已形成許多的空隙,因水慢速結冰,就有足夠的時間讓水分子把質量重密度大的鹽分子全部析出,沉澱在水下,不會包裹在冰晶的空隙裡形成鹽泡,而構成純淨的淡水冰,漂浮在水面上;同理,冰塊、碎冰、冰霜、冰水(液態冰),倘若 溫度皆已達到海水的冰點以下,即-2℃以下,因水分子皆已規則性的排列,且皆已將質量重密度大的鹽分子全部析出,水分子間已膨脹鬆散,體積已大9%,皆同樣具備淡水冰的特質,漂浮在水面上。 "After water freezes into ice, its volume increases by 9%": The water molecules in ice are made up of hydrogen chains, and their -O-H-O- atoms are arranged in a straight line. Due to this regular arrangement, many gaps are formed between the water molecules in ice. Water molecules without hydrogen chains do not have this regular arrangement, and they will try to stack together tightly (close packing). For example, the hydrogen chain bonding rate of water at room temperature is about 50%, while that of ice is 100% (the higher the hydrogen chain bonding rate of water, the more gaps there are between molecules). In other words, ice has a higher regular arrangement than water, so the gaps between ice molecules are larger. Therefore, when the weight of water and ice is the same, the volume of ice is 9% larger. Seawater is salt molecules and water molecules, which are combined in the state of a mixture, that is, combined in a physical state. Its structure is very fragile. Water is composed of two elements, hydrogen and oxygen. The atomic mass of hydrogen is 1.00794u, making it the lightest element in the universe. The atomic mass of oxygen is 15.9994, ranking third after hydrogen and helium. The atomic mass of water is 17.00734. Salt, sodium chloride (NaCl), is composed of two elements, chlorine and sodium. The atomic mass of chlorine is 35.45 and the atomic mass of sodium is 22. .9898, the atomic mass of salt is 58.4398, and the density of salt is 2.165; if seawater freezes slowly, the atomic hydrogen chains of water molecules are regularly arranged in a straight line, and many gaps have been formed between water molecules. Because water freezes slowly, there is enough time for water molecules to precipitate all the salt molecules with heavy mass and density and precipitate them underwater, and they will not be wrapped in the gaps between ice crystals to form salt bubbles. , and pure freshwater ice is formed, floating on the water surface; similarly, ice cubes, crushed ice, frost, and ice water (liquid ice), if the temperature has reached below the freezing point of seawater, that is, below -2℃, because the water molecules have been regularly arranged, and all the salt molecules with high mass density have been precipitated, the water molecules have expanded and loosened, and the volume has increased by 9%, they all have the characteristics of freshwater ice and float on the water surface.
上述〝水分子氫氧鏈結合的構型〞,請參考:北京大學科學家在國家資助下,人類首次拍到水分子的內部氫鍵構型(O-H…O),研究成果發表在本期2022年1月5日以Article的形式在《自然-材料》[Nature Materials DIO:10.1038/nmat3848],既可得到證明。 For the above-mentioned "hydroxide chain bonding configuration of water molecules", please refer to: Scientists from Peking University, with national funding, photographed the internal hydrogen bond configuration of water molecules for the first time (O-H...O). The research results were published in the form of an article in Nature Materials [Nature Materials DIO: 10.1038/nmat3848] on January 5, 2022, which can be proved.
根據國際淡化協會(International Desalination Association,IDA)的統計,迄2013年為止,全世界共建成一萬七千座海水淡化廠,日產淡水八千多萬噸,有3億人生活已離不開淡化的海水了。 According to statistics from the International Desalination Association (IDA), as of 2013, there are 17,000 desalination plants built around the world, producing more than 80 million tons of fresh water per day, and 300 million people cannot live without desalinated seawater.
按,目前海水淡化的〝鹽、水分離法〞,成熟的製程共有二項,其一為〝加熱法〞,其二為〝逆滲透法〞,謹分別說明如下: According to the current "salt-water separation method" for seawater desalination, there are two mature processes, one is the "heating method" and the other is the "reverse osmosis method", which are explained as follows:
一、〝加熱法〞:把海水先蒸發,因水蒸氣不含鹽分再冷卻後即得淡水,以除去鹽分。其中,有多級閃沸、多效蒸發、蒸氣再壓縮等工法。而加熱法需要大量的熱能,生產成本高,產量有限,常與火力發電廠共構,以電廠汽輪機排放的低壓蒸氣做為廉價的能源,產量有限。 1. "Heating method": evaporate the seawater first, because the water vapor does not contain salt, and then cool it to get fresh water to remove the salt. Among them, there are multi-stage flash boiling, multi-effect evaporation, steam recompression and other methods. The heating method requires a lot of thermal energy, high production costs, limited output, and is often co-constructed with thermal power plants, using low-pressure steam emitted by the power plant's steam turbine as a cheap energy source, and the output is limited.
二、〝逆滲透法〞:目前海水淡化以逆滲透法(reverse osmosis,RO)為主,逆滲透法已為海水淡化的生產主流,約有6成的淡化廠採用,且比率逐年提高,其原因是逆滲透法的製程有下列優點:建廠速度快、消耗能源較加熱法少、操作容易,且大型逆滲透海水淡化廠的興建費用與淡水的生產成本也較其他方法低廉使然。 2. "Reverse osmosis": Currently, seawater desalination is mainly based on reverse osmosis (RO). Reverse osmosis has become the mainstream of seawater desalination production, with about 60% of desalination plants adopting it, and the proportion is increasing year by year. The reason is that the reverse osmosis process has the following advantages: fast plant construction speed, less energy consumption than heating method, easy operation, and the construction cost of large-scale reverse osmosis seawater desalination plants and the production cost of fresh water are also lower than other methods.
逆滲透製水法(Reverse Omission,簡稱R.O.)是目前最先 進最有效的淨水處理法,它能有效分離海水中的水分子與鹽分子、鈣、鎂等硬度雜質、重金屬、化學殘留物質、及病毒、細菌等,因而可生產出安全的飲用淡水。 Reverse Osmosis (R.O.) is the most advanced and effective water purification method. It can effectively separate water molecules from salt molecules, hard impurities such as calcium and magnesium, heavy metals, chemical residues, viruses, bacteria, etc. in seawater, thereby producing safe drinking water.
然〝逆滲透製水法〞係針對〝表層海水〞的淡化生產而言,仍有諸多缺失,致產量難以大幅提升,大量生產,降低成本,取代各種水源,廣泛普遍使用。 However, the "reverse osmosis water production method" is aimed at the desalination production of "surface seawater" and still has many shortcomings, making it difficult to significantly increase production, mass produce, reduce costs, replace various water sources, and be widely used.
究其原因:現行逆滲透製水法有下列必要的工序:1、先將海水導入儲存槽儲存。2、經過一套前置過濾系統進行初步過濾。3、過濾水儲存槽儲存已初步過濾的海水。4、經微過濾系統再進一步過濾。5、使用高壓泵浦將已兩度過濾的海水送到逆滲透RO模組進行鹽水分離。6、藉節能設備回收部分能量(利用高壓鹵水的壓力能回收部分能量)。7、淡水儲存槽儲存淡水。8、將淡水輸入自來水系統。9、將鹵水排放入海。 The reason is: the current reverse osmosis water production method has the following necessary processes: 1. First, introduce seawater into the storage tank for storage. 2. Perform preliminary filtration through a pre-filtration system. 3. Store the initially filtered seawater in the filtered water storage tank. 4. Further filter through the micro-filtration system. 5. Use a high-pressure pump to send the twice-filtered seawater to the reverse osmosis RO module for salt-water separation. 6. Recover part of the energy through energy-saving equipment (use the pressure of high-pressure brine to recover part of the energy). 7. Store fresh water in the fresh water storage tank. 8. Input fresh water into the tap water system. 9. Discharge brine into the sea.
上述工序,無法簡化省略,因此有下列的諸多缺失:1、前置過濾和再度微過濾處理系統,耗時耗工故產量難以大幅提升。2、藉高壓泵浦將海水輸入RO膜圓柱筒分離鹵水和淡水相當耗能,成本難以降低。3、透過RO膜圓柱筒分離鹵水和淡水,速度緩慢,難以大量生產。4、深層海水所擁有極端珍貴的礦物質與微量元素,透過逆滲透RO膜過濾法過濾後,將全部剔除殆盡,無法保留。 The above process cannot be simplified or omitted, so there are many deficiencies as follows: 1. The pre-filtration and re-microfiltration treatment system is time-consuming and labor-intensive, so it is difficult to significantly increase the output. 2. Using a high-pressure pump to input seawater into the RO membrane cylinder to separate brine and fresh water is quite energy-consuming, and the cost is difficult to reduce. 3. The separation of brine and fresh water through the RO membrane cylinder is slow and difficult to mass produce. 4. The extremely precious minerals and trace elements in deep seawater will be completely removed after being filtered through the reverse osmosis RO membrane filtration method and cannot be retained.
上述逆滲透製水法的海水淡化生產技術,係針對〝表層海水〞的淡化而言,深層海水迴然不同。深層海水:一般界定為200米至4000米之間的海水。 The above-mentioned reverse osmosis water production method of seawater desalination production technology is aimed at the desalination of "surface seawater", and deep seawater is completely different. Deep seawater: generally defined as seawater between 200 meters and 4,000 meters.
深層海水的優越性可歸納以下五個特質:(資料來源:經濟 部水利產業資訊網;經濟部研擬「深層海水資源利用和產業發展政策綱領」草案送行政院,奉行政院94年4月12日院臺經字第0940011375號函核定,作為我國深層海水產業未來發展之政策指導。) The superiority of deep seawater can be summarized into the following five characteristics: (Source: Ministry of Economic Affairs Water Industry Information Network; the Ministry of Economic Affairs drafted the "Deep Seawater Resource Utilization and Industry Development Policy Guidelines" and sent it to the Executive Yuan, which was approved by the Executive Yuan on April 12, 2005, with the letter No. 0940011375, as a policy guide for the future development of Taiwan's deep seawater industry.)
1、清澈乾淨性:人為的污染不易到達,是構成深層海水潔淨的原因之一。另外,表層海水在沉澱過程中,細菌會因化學酸化、沉澱、漂流擴散等之分解作用,隨深度而逐漸減少,且因深海缺少殘存的有機物質及硝酸體氮素等細菌所需的養份,細菌難以生存繁殖。因此,導致動值物病變的各種有害細菌或病毒,在深層海水中的含量均極為稀少,僅為表層海水的千分之一至萬分之一。再者,殘存於深層海水的有機物,對微生物分解殘渣有機物作用的抵抗性相當安定,這也是深層海水的水質在微生物學或物理化學方面較為安定、無機且清淨的原因。 1. Clearness and cleanliness: It is difficult for artificial pollution to reach deep seawater, which is one of the reasons why deep seawater is clean. In addition, during the sedimentation process of surface seawater, bacteria will gradually decrease with depth due to decomposition effects such as chemical acidification, sedimentation, drift diffusion, etc., and because the deep sea lacks residual organic matter and nitrate nitrogen and other nutrients required by bacteria, it is difficult for bacteria to survive and reproduce. Therefore, the content of various harmful bacteria or viruses that cause animal diseases in deep seawater is extremely rare, only one thousandth to one ten-thousandth of that in surface seawater. Furthermore, the organic matter remaining in deep seawater is quite resistant to the decomposition of residual organic matter by microorganisms, which is why the water quality of deep seawater is relatively stable, inorganic and clean in terms of microbiology or physical chemistry.
2、無機營養豐厚性:或稱為「富營養鹽性」,簡單說就是:富含「無機營養鹽類」。據美、日等研究深層海水的專家表示,深層海水所含的氮、磷、矽、硝酸等無機營養鹽,平均比表層海水高出數倍到數拾倍。由於光線不足,光合作用幾乎無法進行,因此植物性浮游生物所需的必要營養鹽-氮、磷、矽、硝酸等都無法消耗,大量累積在深層海水中,成為營養特別豐富的水,這種特性就稱為「無機營養豐厚性」。 2. Rich in inorganic nutrients: or "rich in nutrients", in simple terms: rich in "inorganic nutrients". According to experts in the United States and Japan who study deep seawater, the inorganic nutrients such as nitrogen, phosphorus, silicon, and nitric acid contained in deep seawater are several to dozens of times higher than those in surface seawater on average. Due to insufficient light, photosynthesis is almost impossible, so the necessary nutrients required by plant plankton - nitrogen, phosphorus, silicon, nitric acid, etc. cannot be consumed, and a large amount of them accumulate in deep seawater, becoming water with particularly rich nutrients. This characteristic is called "rich in inorganic nutrients".
3、低溫安定性:深層海水由於位在光線無法照到的深海中,水溫比表層海水的水溫低,而且幾乎一整年都沒有變化,低溫的情況非常穩定,所以可規劃做為多種用途,如:溫差發電、養殖冷水魚類等;其他待開發的冷能用途還有很多。 3. Low temperature stability: Because deep seawater is located in the deep sea where light cannot reach, the water temperature is lower than that of surface seawater and remains almost unchanged throughout the year. The low temperature is very stable, so it can be planned for a variety of uses, such as temperature difference power generation, breeding of cold water fish, etc. There are many other uses of cold energy to be developed.
4、微量礦物質特性:若將深層海水的的水分、鹽分和礦物 質分離,即能萃取出高成分的礦物質與微量元素;礦物質包括:鎂、鈣、鉀等,微量元素包含:鋅、銅、硼、磷、硒等共多達八十多種。就醫療功能而言,鎂與鈣可用以預防骨質疏鬆、疏緩糖尿病及高血壓等病症之功能,也有抑制中性脂肪膽固醇上升之作用。微量元素中,最可貴的是硒,因為日常生活中不容易攝取得到,而人體一旦缺乏硒,則罹患心臟病、糖尿病、癌症的機率相對提高。深層海水中含量豐富的微量元素硒,正好可以彌補人體之不足,對人體健康有莫大的幫助。 4. Characteristics of trace minerals: If the water, salt and minerals in deep seawater are separated, high-content minerals and trace elements can be extracted; minerals include magnesium, calcium, potassium, etc., and trace elements include zinc, copper, boron, phosphorus, selenium, etc., totaling more than 80 kinds. In terms of medical functions, magnesium and calcium can be used to prevent osteoporosis, relieve diabetes and high blood pressure, and also inhibit the rise of neutral fat cholesterol. Among trace elements, the most valuable is selenium, because it is not easy to obtain in daily life. Once the human body lacks selenium, the probability of suffering from heart disease, diabetes and cancer is relatively increased. The trace element selenium, which is rich in deep sea water, can just make up for the deficiency of the human body and is of great help to human health.
5、水分子熟成性:從海平面300公尺以下的海水,因常年處於低溫高壓之環境下,其水分子結構偏小,屬準奈米級之微細分子,且其分子結構穩定,水分子間不易重組結合,因此極具穩定與微小分子結構之特性。 5. Maturity of water molecules: Seawater below 300 meters below sea level is in a low temperature and high pressure environment all year round, so its water molecule structure is relatively small and belongs to quasi-nano-level micro-molecules. Its molecular structure is stable and it is not easy for water molecules to recombine and combine. Therefore, it has the characteristics of extremely stable and micro-molecular structure.
隨著科技的發達,影響人類最重大的議題之一,就是水資源的匱乏問題。然水資源的開發,人類雖已利用海水淡化的技術生產民生用水,然僅止於抽取〝表層海水〞進行淡化,造福小部分人群;但最有價值、最重要,佔地球水資源95%的低溫、富營養、最肥沃的〝深層海水〞的開發,雖美、日和我國,已有小規模在生產,然迄今仍未找到可低成本、大規模、有效率,以物理方法快速大量生產〝淡水〞和〝鹵水〞,並保存深層海水極端珍貴的礦物質和微量元素,有效取代現有水源,廣泛做為民生用水、農業用水、工業用水,以維護人類的健康,改善人類的體質,延長人類的壽命;讓低溫的海淡水,普灑大地,降低土壤溫度,改善土質,治理沙漠,使大地遍地變成黑土,廣增糧食,解決地球暖化危機,維護動植物生存環境,之可行有效辦法,實已刻不容緩,急待解決。 With the development of science and technology, one of the most important issues affecting mankind is the scarcity of water resources. Although humans have used seawater desalination technology to produce water for domestic use, they have only extracted "surface seawater" for desalination, benefiting a small number of people. However, the most valuable and important "deep seawater" that accounts for 95% of the earth's water resources is low-temperature, nutrient-rich, and the most fertile. Although the United States, Japan, and my country have already produced it on a small scale, they have not yet found a low-cost, large-scale, efficient, physical method to quickly produce large quantities of "fresh water" and "halite" and preserve it. The extremely precious minerals and trace elements in deep seawater can effectively replace existing water sources and be widely used as water for people's livelihood, agriculture and industry to maintain human health, improve human physique and prolong human life. It is urgent to let low-temperature seawater sprinkle on the earth, reduce soil temperature, improve soil quality, control deserts, turn the earth into black soil, increase food, solve the global warming crisis and maintain the living environment of animals and plants. It is a feasible and effective method that cannot be delayed and needs to be solved urgently.
有鑑於此,如何利用現代科技,大量低廉生產深層海淡水,取代現有水源,發揮深層海水的五大特質,造福人類和所有動植物,解決水資源匱乏危機,地球暖化危機,糧食不足危機,實為水資源開發重中之重的關鍵課題。豈可將地球95%的低溫、富營養、最肥沃的深層海水,閒置大海,棄之不用,讓水資源不足,人類彼此爭奪,互相殘殺,永無寧日。 In view of this, how to use modern technology to produce a large amount of deep sea fresh water at a low cost to replace the existing water sources, give full play to the five characteristics of deep sea water, benefit mankind and all animals and plants, and solve the water shortage crisis, global warming crisis, and food shortage crisis, is indeed a key issue of the top priority in water resource development. How can we leave 95% of the earth's low-temperature, nutrient-rich, and most fertile deep sea water idle in the sea and abandon it, so that water resources are insufficient, humans compete with each other, kill each other, and there will be no peace forever.
本發明〝深層海水淡化民生用水大量生產系統〞,有效解決上述深層海水低廉大量生產的所有難題,得發揮深層海水的五大特質,取代各式不含礦物質和微量元素的水源,做為民生用水,以維護人類的健康,改善人類的體質,延長人類的壽命。 This invention, "Deep Seawater Desalination Water Mass Production System", effectively solves all the above-mentioned difficulties in the low-cost mass production of deep seawater. It can give full play to the five major characteristics of deep seawater and replace various water sources without minerals and trace elements as water for people's livelihood, so as to maintain human health, improve human physique and prolong human life.
技術方案:本發明為達成上述目的及其功效,公開一種〝深層海水淡化民生用水大量生產系統〞,包括:一發電系統、一虹吸管機構、一抽水機構、一海水儲存池、至少二高壓重力沉澱池、至少二第一鹽水分離機/或至少二第二鹽水分離機、一淡水儲存池、一鹵水儲存池,其中:所述發電系統:係發明人所發明的「海浪浮力和地心引力發電系統」,貴局於2020年5月1日核准發明第I692580號,做為本〝深層海水淡化民生用水大量生產系統〞的電源設備,有效解決耗能大、成本高、大量生產所面臨的成本問題。 Technical solution: In order to achieve the above-mentioned purpose and its effect, the present invention discloses a "deep seawater desalination and domestic water mass production system", including: a power generation system, a siphon mechanism, a pumping mechanism, a seawater storage tank, at least two high-pressure gravity sedimentation tanks, at least two first brine separators/or at least two second brine separators, a freshwater storage tank, and a brine storage tank, wherein: the power generation system: is the "wave buoyancy and gravity power generation system" invented by the inventor. Your Bureau approved the invention No. I692580 on May 1, 2020, as the power supply equipment of this "deep seawater desalination and domestic water mass production system", which effectively solves the cost problems faced by large energy consumption, high cost, and mass production.
所述虹吸管機構:係藉該虹吸管機構的虹吸原理,長臂虹吸管往下延伸600米直接深入深層的海裡,往上再延伸跨越所述海水儲存池的牆壁頂端才轉彎,短臂虹吸管則往下延伸到該海水儲存池底;倘短臂虹吸管管內的液面,比長臂虹吸管管內的液面為低時,則,當虹吸管藉抽水機 構的一抽水機,將水抽入該海水儲存池裡,整條虹吸管已灌滿海水後,虹吸作用已成立,隨即關掉該抽水機,深層海水仍然會經由虹吸管繼續流到該海水儲存池裡,不會停止流動;倘短臂虹吸管管內的液面,比長臂虹吸管管內的液面為高時,則,該海水儲存池裡的海水將會倒流回深層的海裡;此時,必須藉助該抽水機構的抽水機將深層海水抽入該海水儲存池裡;所述抽水機構:係應用該抽水機構的抽水機,補強該虹吸管機構的虹吸作用力不足時使用;即,在該虹吸管機構的短臂虹吸管管內的液面,比長臂虹吸管管內的液面高,無法藉助虹吸作用力將水抽入該海水儲存池時,得啟動該抽水機構的抽水機,將水抽入該海水儲存池裡;也就是,利用該虹吸管機構的虹吸作用力,節省該抽水機構的抽水機能源的消耗量,而達節能的效果。 The siphon mechanism: The long arm siphon extends 600 meters downward directly into the deep sea, and then extends upward to cross the top of the wall of the seawater storage tank before turning, and the short arm siphon extends downward to the bottom of the seawater storage tank; if the liquid level in the short arm siphon is lower than the liquid level in the long arm siphon, then when the siphon pumps water into the seawater storage tank by a pump of the pumping mechanism, the whole siphon is filled with seawater, and the siphon effect is established. When the pump is turned off, the deep seawater will continue to flow into the seawater storage tank through the siphon and will not stop flowing; if the liquid level in the short arm siphon is lower than the liquid level in the long arm siphon, the siphon will stop flowing. When the liquid level is high, the seawater in the seawater storage tank will flow back to the deep sea. At this time, the deep seawater must be pumped into the seawater storage tank by means of the pumping mechanism. The pumping mechanism is used to supplement the insufficient siphon force of the siphon mechanism. That is, when the liquid level in the short arm siphon tube of the siphon mechanism is higher than the liquid level in the long arm siphon tube, and the water cannot be pumped into the seawater storage tank by means of the siphon force, the pumping mechanism must be started to pump water into the seawater storage tank. That is, the siphon force of the siphon mechanism is used to save the energy consumption of the pumping mechanism, thereby achieving the effect of energy saving.
所述海水儲存池:長度與所述高壓重力沉澱池相同,然容量必須比該高壓重力沉澱池的容量大;由於重量太大,為確保結構安全,該海水儲存池必須部分深入地下,以策安全;該海水儲存池的底部,設多根大口徑的輸水管,直通該高壓重力沉澱池的底部;每根輸水管的進水口設一進水電動閘門,一抽水機,可快速將該高壓重力沉澱池灌滿。 The seawater storage tank: has the same length as the high-pressure gravity sedimentation tank, but its capacity must be larger than that of the high-pressure gravity sedimentation tank; due to its heavy weight, the seawater storage tank must be partially buried underground to ensure structural safety; at the bottom of the seawater storage tank, there are multiple large-caliber water pipes that directly connect to the bottom of the high-pressure gravity sedimentation tank; at the water inlet of each water pipe, there is an electric water inlet gate and a pump to quickly fill the high-pressure gravity sedimentation tank.
所述該高壓重力沉澱池:至少設二個,即,第一高壓重力沉澱池/及第二高壓重力沉澱池,其容量依淡水每日的需求量設置,倘日產需求量為45萬噸,則該高壓重力沉澱池的容量既設為45萬噸,即,長300米、寬50米、高30米;在該第一高壓重力沉澱池/及該第二高壓重力沉澱池的高20米處,設一半透膜隔離板,將該第一高壓重力沉澱池/及該第二高壓重力沉澱池分隔成:第一下池/及第二下池、第一上池/及第二上池; 該第一下池/及該第二下池:係由該半透膜隔離板到該第一高壓重力沉澱池/及該第二高壓重力沉澱池的底部所構成,即水深10米~30米的範圍;此部分,水的重力壓強P=2大氣壓P0~4大氣壓P0,在此一高壓重力的環境下進行沉澱,讓有毒的重金屬、硬度雜質、化學殘留物質等受地心引力的影響快速沉澱,倘這些質量重粒子粗的重金屬、硬度雜質、化學殘留物質,違反自然法則,往上攀升穿越該半透膜隔離板時,因該半透膜隔離板位於水深10米處,其下壓力=側壓力=上壓力=2大氣壓P0,將會以2大氣壓P0的下壓力協助該半透膜隔離板從上把它擋住、也會以2大氣壓P0的側壓力協助該半透膜隔離板從旁把它推走、再加上這些物質本身的重力受地心引力往下拉、以及該半透膜隔離板奈米級的孔徑阻截,質量重粒子粗的重金屬、硬度雜質、化學殘存物質,實難往上攀升硬闖穿越該半透膜隔離板而成漏網之魚,進入該第一上池/或該第二上池裡;該第一下池/或該第二下池的底部由該海水儲存池直接延伸過來的多根輸水管往下轉彎,出口處設一出水電動閘門;該第一高壓重力沉澱池/及該第二高壓重力沉澱池的底部外側,設一排水電動閘門、一海水排水管直通海裡;該第一上池/及該第二上池:係由該半透膜隔離板到該第一高壓重力沉澱池/及該第二高壓重力沉澱池的頂部所構成,即水面~水深10米的範圍;此部分,設多根大口徑的輸水管,每根輸水管的進水口設一進水電動閘門、一半透膜隔離管、一抽水機;該第一上池/及該第二上池的出水總流量等於該第一下池/及該第二下池的進水總流量,使該第一高壓重力沉澱池/及該第二高壓重力沉澱池的水位始終保持不變;該半透膜隔離管的半透膜和該半透膜隔離板的半透膜一樣,僅過濾有毒的重金屬、硬度雜質、 化學殘留物質外,鹽、水、礦物質和微量元素全部讓其通過,送給所述第一鹽水分離機/或所述第二鹽水分離機,應用冷凍法進行鹽、水、礦物質和微量元素等的分離。 The high-pressure gravity sedimentation tanks are provided with at least two, i.e., the first high-pressure gravity sedimentation tank and the second high-pressure gravity sedimentation tank, and the capacity thereof is set according to the daily demand for fresh water. If the daily demand is 450,000 tons, the capacity of the high-pressure gravity sedimentation tank is set to 450,000 tons, i.e., 300 meters in length, 50 meters in width, and 30 meters in height; a semi-permeable membrane separation plate is provided at a height of 20 meters of the first high-pressure gravity sedimentation tank and the second high-pressure gravity sedimentation tank to separate the first high-pressure gravity sedimentation tank and the second high-pressure gravity sedimentation tank into: a first lower tank and a second lower tank, a first upper tank and a second upper tank; The first lower pool and the second lower pool are composed of the semipermeable membrane isolation plate to the bottom of the first high-pressure gravity sedimentation tank and the second high-pressure gravity sedimentation tank, i.e., the water depth is 10 meters to 30 meters; in this part, the gravity pressure of the water is P = 2 atmospheres P 0 ~ 4 atmospheres P 0 In this high-pressure gravity environment, precipitation is carried out, allowing toxic heavy metals, hard impurities, chemical residues, etc. to settle quickly under the influence of gravity. If these heavy metals, hard impurities, chemical residues with heavy mass and coarse particles violate the laws of nature and climb upward through the semipermeable membrane isolation plate, because the semipermeable membrane isolation plate is located at a depth of 10 meters, its lower pressure = side pressure = upper pressure = 2 atmospheres P 0 , it will use a lower pressure of 2 atmospheres P 0 to assist the semipermeable membrane isolation plate to block it from above, and will also use 2 atmospheres P The side pressure of 0 assists the semipermeable membrane isolation plate to push it away from the side, and the gravity of these substances themselves is pulled downward by the earth's gravity, and the nano-scale pore size of the semipermeable membrane isolation plate blocks heavy metals with heavy mass and coarse particles, hard impurities, and chemical residual substances. It is difficult for them to climb up and penetrate through the semipermeable membrane isolation plate, and they slip into the first upper pool/or the second upper pool. The bottom of the first lower pool/or the second lower pool is directly extended from the seawater storage tank. The multiple water pipes turn downward, and an electric water gate is set at the outlet; the outer side of the bottom of the first high-pressure gravity sedimentation tank/and the second high-pressure gravity sedimentation tank is provided with a drainage electric gate and a seawater drainage pipe directly connected to the sea; The first upper pool/and the second upper pool: are formed from the semipermeable membrane isolation plate to the top of the first high-pressure gravity sedimentation tank/and the second high-pressure gravity sedimentation tank, i.e., the range from the water surface to a water depth of 10 meters; in this part, a plurality of large-caliber water pipes are provided, and the water inlet of each water pipe is provided with an inlet electric gate, a semipermeable membrane isolation pipe, and a pump; the total outflow of the first upper pool/and the second upper pool is equal to the total inflow of the first lower pool/and the second lower pool, so that the water level of the first high-pressure gravity sedimentation tank/and the second high-pressure gravity sedimentation tank always remains unchanged; the semipermeable membrane of the semipermeable membrane isolation pipe is the same as the semipermeable membrane of the semipermeable membrane isolation plate, and only filters toxic heavy metals, hard impurities, Except for chemical residues, salt, water, minerals and trace elements are all allowed to pass through and sent to the first salt water separator/or the second salt water separator, and the salt, water, minerals and trace elements are separated by freezing method.
該第一高壓重力沉澱池/及該第二高壓重力沉澱池:必須二個一起灌滿後,才可開始使用;每天使用一個,另一個清洗乾淨重灌沉澱一天後,隔天才使用;也就是,今天使用新池,昨天已用過的舊池,將該舊池的外側,該海水排水管的該排水電動閘門的開關打開,把該舊池的汙水全部經由該海水排水管直接排入海裡;當該舊池往下不斷排水,該第一下池/或該第二下池的汙水很快就排光,該第一上池/或該第二上池乾淨的水自然垂直往下流,水重力自然全部往下壓快速沖刷清洗該半透膜隔離板,緊接著再把該第一下池/或該第二下池也沖刷清洗乾淨;此時,所述淡水儲存池,設一半透膜清洗管、一清洗電動閘門;該半透膜清洗管從該淡水儲存池連接到該第一上池/及該第二上池的每根該半透膜隔離管的上面,隨即打開該半透膜清洗管的該清洗電動閘門的開關,開始往下噴水快速沖洗該半透膜隔離管;待該半透膜隔離管、該半透膜隔離板、該第一下池/或該第二下池,全部沖刷清洗乾淨,把水洩光;才關上該海水排水管的該排水電動閘門的開關,開始重新進水將該舊池灌滿;兩個高壓重力沉澱池,周而復始,來回更換,每天都把該半透膜隔離管、該半透膜隔離板、該第一下池/或該第二下池,全部沖刷清洗乾淨,才重新灌水使用,因此,該半透膜隔離管、該半透膜隔離板,該第一下池/及該第二下池,始終保持乾淨,不會阻塞,以確保系統穩定通暢運行。 The first high-pressure gravity sedimentation tank/and the second high-pressure gravity sedimentation tank: Both must be filled up before they can be used; one is used every day, and the other is cleaned and refilled for sedimentation for one day before being used the next day; that is, the new tank is used today, and the old tank that was used yesterday is used. The switch of the drainage electric gate of the seawater drainage pipe on the outside of the old tank is opened, and all the sewage in the old tank is discharged directly into the sea through the seawater drainage pipe; When the old pool is continuously drained, the sewage in the first lower pool/or the second lower pool is quickly drained, and the clean water in the first upper pool/or the second upper pool naturally flows vertically downward, and the water gravity naturally presses all downward to quickly flush and clean the semipermeable membrane isolation plate, and then flush and clean the first lower pool/or the second lower pool; at this time, the fresh water storage tank is provided with a semipermeable membrane cleaning pipe and a cleaning electric gate; the semipermeable membrane cleaning pipe is connected from The fresh water storage tank is connected to the top of each semipermeable membrane isolation pipe of the first upper tank/and the second upper tank, and the switch of the cleaning electric gate of the semipermeable membrane cleaning pipe is immediately turned on to start spraying water downward to quickly flush the semipermeable membrane isolation pipe; after the semipermeable membrane isolation pipe, the semipermeable membrane isolation plate, the first lower tank/or the second lower tank are all flushed and cleaned, and the water is drained; the switch of the drainage electric gate of the seawater drainage pipe is closed. , start to refill the old pool with water; the two high-pressure gravity sedimentation tanks are replaced back and forth over and over again. Every day, the semipermeable membrane isolation tube, the semipermeable membrane isolation plate, the first lower pool/or the second lower pool are all flushed and cleaned before refilling with water. Therefore, the semipermeable membrane isolation tube, the semipermeable membrane isolation plate, the first lower pool/and the second lower pool are always kept clean and will not be blocked to ensure stable and smooth operation of the system.
根據經濟部水利產業資訊網公布:深層海水優越性的五大特 質,請參考本說明書【0016】節:「1、清澈乾淨性:人為的污染不易到達,是構成深層海水潔淨的原因之一。另外,表層海水在沉澱過程中,細菌會因化學酸化、沉澱、漂流擴散等之分解作用,隨深度而逐漸減少,且因深海缺少殘存的有機物質及硝酸體氮素等細菌所需的養份,細菌難以生存繁殖。因此,導致動植物病變的各種有害細菌或病毒,在深層海水中的含量均極為稀少,僅為表層海水的千分之一至萬分之一。再者,殘存於深層海水的有機物,對微生物分解殘渣有機物作用的抵抗性相當安定,這也是深層海水的水質在微生物學或物理化學方面較為安定、無機且清淨的原因。」 According to the Ministry of Economic Affairs' Water Conservancy Industry Information Network, the five superior characteristics of deep seawater are listed in Section [0016] of this manual: "1. Clarity and cleanliness: It is difficult for artificial pollution to reach deep seawater, which is one of the reasons why deep seawater is clean. In addition, during the sedimentation process of surface seawater, bacteria will gradually decrease with depth due to decomposition effects such as chemical acidification, sedimentation, drift diffusion, etc., and because the deep sea lacks residual organic matter and nitrate nitrogen, etc. The nutrients required by bacteria make it difficult for them to survive and reproduce. Therefore, the content of various harmful bacteria or viruses that cause animal and plant diseases in deep seawater is extremely rare, only one thousandth to one ten-thousandth of that in surface seawater. Furthermore, the organic matter remaining in deep seawater is quite resistant to the decomposition of residual organic matter by microorganisms, which is why the water quality of deep seawater is relatively stable, inorganic and clean in terms of microbiology or physical chemistry. ”
綜上所述,深層海水本已相當乾淨,縱使還有微少的殘存重金屬、硬度雜質,或化學殘存物質,也可藉該高壓重力沉澱池以高壓重力的方式快速沉澱,並藉該半透膜隔離板及該半透膜隔離管奈米級的孔徑阻截而加以排除。 In summary, deep seawater is already quite clean. Even if there are still traces of residual heavy metals, hard impurities, or chemical residues, they can be quickly precipitated by high-pressure gravity in the high-pressure gravity sedimentation tank and removed by the nano-scale pores of the semipermeable membrane isolation plate and the semipermeable membrane isolation tube.
由於現有表層海水淡化系統使用逆滲透RO膜分離淡水與鹵水,連同極其珍貴的礦物質及微量元素也一併排除,致生產出來的淡水已無營養,頗為可惜;因此,該半透膜隔離板及該半透膜隔離管所使用的半透膜,其孔徑不宜太微細,除可排除重金屬、硬度雜質、化學殘留物質等質量重粒子粗的有毒物質外,深層海水所含豐厚的礦物質包括:鎂、鈣、鉀等,及微量元素包含:鋅、銅、硼、磷、硒等八十多種元素,皆已和水分子及鹽分子,常年處於低溫高壓的深層海裡,分子結構已偏小、穩定,分子間已不易重組結合,極具穩定與微小之分子結構特性(請參考:本說明書第【0017】、【0018】、【0019】、【0020】各節的說明既明);因此必須保存這些珍貴的營養品穿越該半透膜隔離板及該半透膜隔離管進入該第一鹽水分 離機裡,不能將其排除;目前半透膜的成品較適合的有;1、RO膜(reverse osmosis):透水孔徑0.0001~0.002micron。2、NF膜(nanofiltration);透水孔徑0.0009~0.009micron;3、UF膜(ultrafiltration):透水孔徑0.006~0.11micron;4、MF膜(microfiltration):透水孔徑0.08~1.2micron;還有很多,謹摘錄較適合的部分提供參考。在所有半透膜的項目中唯有逆滲透RO膜的透水孔徑最小,在0.0001~0.002micron之間,如以人體頭髮做比較,人體頭髮之外徑約為10micron,即可知逆滲透RO膜孔徑之精密;然該高壓重力沉澱池的目的,僅作為排除深層海水殘存質量重粒子粗的重金屬、硬度雜質、和化學殘留物質,故採用透水孔徑較粗的第3項UF膜透水孔徑0.006~0.11micron,或第4項MF膜透水孔徑0.08~1.2micron,才能保存這些珍貴的營養品。 Since the existing surface seawater desalination system uses reverse osmosis RO membrane to separate fresh water and brine, it also removes extremely precious minerals and trace elements, resulting in the fresh water produced having no nutrients, which is a pity. Therefore, the pore size of the semipermeable membrane used in the semipermeable membrane isolation plate and the semipermeable membrane isolation tube should not be too fine. In addition to removing heavy metals, hard impurities, chemical residues and other heavy and coarse toxic substances, the deep seawater contains rich minerals including magnesium, calcium, potassium, etc., and trace elements including zinc, copper, boron, phosphorus, selenium and more than 80 elements, all of which are The water molecules and salt molecules have been in the deep sea with low temperature and high pressure for many years. The molecular structure is small and stable. It is not easy for the molecules to recombine and combine. It has the characteristics of stable and tiny molecular structure (please refer to the description of Sections [0017], [0018], [0019], and [0020] of this manual). Therefore, these precious nutrients must be preserved and pass through the semipermeable membrane isolation plate and the semipermeable membrane isolation tube into the first salt water separator. They cannot be discharged. The semipermeable membrane products that are more suitable are: 1. RO membrane (reverse osmosis): the water permeability is 0.0001~0.002 micron. 2. NF membrane (nanofiltration): pore size 0.0009~0.009 micron; 3. UF membrane (ultrafiltration): pore size 0.006~0.11 micron; 4. MF membrane (microfiltration): pore size 0.08~1.2 micron; There are many more, I would like to extract the more suitable parts for reference. Among all the semipermeable membranes, only the reverse osmosis RO membrane has the smallest pore size, which is between 0.0001 and 0.002 microns. If we compare it to human hair, the outer diameter of human hair is about 10 microns, which shows the precision of the pore size of the reverse osmosis RO membrane. However, the purpose of the high-pressure gravity sedimentation tank is only to remove the heavy metals, hardness impurities, and chemical residues with heavy mass and coarse particles from the deep seawater. Therefore, the third item UF membrane with a coarser pore size of 0.006~0.11 microns or the fourth item MF membrane with a pore size of 0.08~1.2 microns is used to preserve these precious nutrients.
所述第一鹽水分離機:設內外兩層外殼,該外層外殼:設一層保溫膜、一冷凍壓縮機、一溫度控制器;該保溫膜:可隔絕外面的溫度,保持機內的溫度恆溫;該冷凍壓縮機:可提供冷氣維持機內-2℃~-20℃的恆溫環境;該溫度控制器:可隨意設定機內的恆溫度數;該內層外殼:設一旋轉桶,該旋轉桶由一第二馬達,帶動一第二傳動齒輪,轉動該旋轉桶旋轉;該旋轉桶的桶壁設許多細密的小孔,其內層的桶壁緊貼一層半透膜,水分子、礦物質和微量元素質量輕粒子細的分子,可透過該半透膜由桶壁的細孔外溢;鹽分子、礦物質和微量元素質量重粒子粗的分子,無法透過該半透膜外溢;該旋轉桶的中心設一葉片輪,該葉片輪的上下設兩個軸承以固定該葉片輪,幫助該葉片輪穩定旋轉;該葉片輪由一第一馬達,帶動一第一傳動齒輪,轉動該葉片輪旋轉;該第一鹽水分離機的上面設一進水管,該進水管設一進水電 動閘門、一噴霧龍頭;當該進水管的該進水電動閘門的開關打開,該噴霧龍頭可將海水調成噴霧狀往下噴灑進水;因深層海水的溫度本就維持在4℃~7℃左右的低溫,機內恆溫的度數設定在-2℃~-20℃海水冰點以下的度數,噴出的水霧機內的冷空氣很容易滲透進水霧中的小水滴裡,使小水滴快速降溫冷卻到冰點-2℃以下的度數,而變成冰水(液態冰);當該噴霧龍頭開始噴出水霧進水時,該第一鹽水分離機的該第一馬達,帶動該第一傳動齒輪,轉動該葉片輪快速旋轉,使該噴霧龍頭噴進來的冰水跟著該葉片輪快速流動,冰水才不會瞬間結冰,維持液態冰的狀態持續流動;設該第一鹽水分離機的容量為3噸,且1分鐘灌滿3噸的海水,當海水灌滿時,該進水管的該進水電動閘門的開關隨即關閉,該葉片輪再持續旋轉10~20秒,確定水分子已全部變成冰水;此時,該第二馬達,帶動該第二傳動齒輪,轉動該旋轉桶快速旋轉,將水分子已膨脹鬆散的冰水,藉該旋轉桶的離心力將水分子、礦物質和微量元素質量輕粒子細的分子,甩出該旋轉桶的外層外殼的桶裡;而鹽分子、礦物質和微量元素質量重粒子粗的分子,被該旋轉桶的該半透膜阻截而留在該旋轉桶裡;當水分子、礦物質和微量元素質量輕粒子細的分子,全部甩出該旋轉桶外,儲存在該外層外殼桶底後,隨即藉一淡水電動閘門把淡水輸水管的開關打開,將淡水全部輸送到所述淡水儲存池裡;此時,儲存在該旋轉桶裡的鹵水,即鹽分子、礦物質和微量元素質量重粒子粗的分子,隨即藉一鹵水電動閘門把鹵水輸水管的開關打開,將鹵水全部輸送到所述鹵水儲存池裡,估計全部行程約2分鐘。 The first salt-water separator is provided with an inner and outer shell. The outer shell is provided with a heat preservation film, a refrigeration compressor and a temperature controller. The heat preservation film can isolate the outside temperature and keep the temperature inside the machine constant. The refrigeration compressor can provide cold air to maintain a constant temperature environment of -2°C to -20°C inside the machine. The temperature controller can set the constant temperature inside the machine at will. The inner shell is provided with a heat preservation film, a refrigeration compressor and a temperature controller. A rotating barrel, the rotating barrel is driven by a second motor, driving a second transmission gear to rotate the rotating barrel; the barrel wall of the rotating barrel is provided with many fine holes, and the inner barrel wall is closely attached to a semipermeable membrane, and water molecules, minerals and trace elements with light and fine particles can pass through the semipermeable membrane and overflow from the fine holes of the barrel wall; salt molecules, minerals and trace elements with heavy and coarse particles cannot The water overflows through the semipermeable membrane; a blade wheel is arranged at the center of the rotary barrel, and two bearings are arranged above and below the blade wheel to fix the blade wheel and help the blade wheel to rotate stably; the blade wheel is driven by a first motor to drive a first transmission gear to rotate the blade wheel; a water inlet pipe is arranged on the top of the first salt-water separator, and the water inlet pipe is provided with a water inlet electric gate and a spray faucet; when the water inlet pipe The switch of the water inlet electric gate is turned on, and the spray faucet can adjust the seawater to spray downward into the water; because the temperature of deep seawater is originally maintained at a low temperature of about 4℃~7℃, the temperature inside the machine is set at -2℃~-20℃ below the freezing point of seawater. The cold air in the spray water mist machine can easily penetrate into the small water droplets in the water mist, causing the small water droplets to quickly cool down to the freezing point -2℃. ℃ or below, and turns into ice water (liquid ice); when the spray faucet starts to spray water, the first motor of the first salt water separator drives the first transmission gear to rotate the impeller wheel quickly, so that the ice water sprayed from the spray faucet flows quickly along with the impeller wheel, so that the ice water will not freeze instantly and maintain the state of liquid ice and continue to flow; the first salt water separator The capacity is 3 tons, and it takes 1 minute to fill up with 3 tons of seawater. When the seawater is filled up, the switch of the water inlet electric gate of the water inlet pipe is immediately closed, and the impeller continues to rotate for 10 to 20 seconds to make sure that all the water molecules have turned into ice water. At this time, the second motor drives the second transmission gear to rotate the rotating barrel quickly, and the ice water with expanded and loosened water molecules is pushed into the water by the centrifugal force of the rotating barrel. Water molecules, minerals and trace elements with light and fine mass are thrown out of the outer shell of the rotating barrel; while salt molecules, minerals and trace elements with heavy and coarse mass are intercepted by the semipermeable membrane of the rotating barrel and remain in the rotating barrel; when all water molecules, minerals and trace elements with light and fine mass are thrown out of the rotating barrel and stored at the bottom of the outer shell, That is, a fresh water electric gate opens the switch of the fresh water pipe to transport all the fresh water to the fresh water storage tank; at this time, the brine stored in the rotating barrel, that is, the heavy and coarse molecules of salt molecules, minerals and trace elements, is immediately opened by a brine electric gate to transport all the brine to the brine storage tank. The entire journey is estimated to take about 2 minutes.
該第一鹽水分離機:裝設排數和台數,係依照淡水每天的需 求量設置;倘該第一鹽水分離機每台的容量設為3噸,2分鐘輸出一次,即每分鐘生產1.5噸;則,配合該高壓重力沉澱池日產量設為45萬噸計算:需安裝:450000噸÷24時÷60分÷1.5噸/分=209台,則,設11排,每排21台,共安裝231台,多安裝了1排21台,係每天逐排停機一次,沖刷清洗該第一鹽水分離機的該半透膜,避免阻塞影響生產出來的淡水品質;該高壓重力沉澱池配合該第一鹽水分離機的裝設排數,設11根大口徑的輸水管,直接穿越該11排的該第一鹽水分離機的上面,使用三向接頭往下與該第一鹽水分離機的該進水管連接;該進水管的該噴霧龍頭,亦可調整改變噴水的模式噴出水刀,該第一鹽水分離機每天逐排停機一次,讓該噴霧龍頭朝下方的四周噴出水刀,沖刷清洗機內的該半透膜,以免阻塞,影響生產出來的淡水品質。 The first salt water separator: the number of rows and units installed is set according to the daily demand for fresh water; if the capacity of each first salt water separator is set to 3 tons, and the output is once every 2 minutes, that is, 1.5 tons per minute; then, with the daily output of the high-pressure gravity sedimentation tank set to 450,000 tons, the following calculation is required: 450,000 tons ÷ 24 hours ÷ 60 minutes ÷ 1.5 tons/minute = 209 units need to be installed, then 11 rows are set, 21 units per row, a total of 231 units are installed, and 1 row of 21 units are installed extra, which means that the first salt water separator is shut down once a day to flush and clean the semipermeable membrane, avoiding Blockage affects the quality of the produced fresh water; the high-pressure gravity sedimentation tank is equipped with 11 large-caliber water pipes in accordance with the number of rows of the first salt water separator, which directly pass through the top of the 11 rows of the first salt water separator and are connected to the water inlet pipe of the first salt water separator downward using a three-way joint; the spray faucet of the water inlet pipe can also be adjusted to change the spray mode to spray water jets. The first salt water separator is shut down once a day, row by row, so that the spray faucet sprays water jets around the bottom to flush the semi-permeable membrane in the cleaning machine to avoid blockage and affect the quality of the produced fresh water.
有關該第一鹽水分離機的操作原理,請參考本說明書【0004】節的說明既明:「〝水結成冰後,體積增加9%〞:冰的水分子是由氫氧鏈結合而成,其-O-H-O-原子排列在一直線上,由於這個規則性的排列關係,冰的水分子間形成許多的空隙;而沒有氫鏈結合的水分子,就沒有這種規則性的排列,它會盡量的緊密堆積在一起(close packing)。如室溫的水,其氫鏈結合率約為50%,而冰為100%(氫鏈結合比率越高的水,分子間的空隙就越多),也就是,冰較水規則性的排列高,所以冰的分子間空隙大,因此水和冰的重量相同時,冰的體積大9%;而海水乃是鹽分子和水分子,以混合物的狀態相結合,也就是,以物理狀態結合,其結構非常脆弱;而水是由氫、氧兩種元素組成,氫原子質量為1.00794u,是宇宙最輕的元素,氧原子質量為15.9994,僅次於氫和氦,佔第三位,水的原子質量為17.00734;而鹽, 氯化鈉NaCl,是由氯、鈉兩種元素組成,氯原子質量為35.45,鈉原子質量為22.9898,鹽的原子質量為58.4398,鹽的密度為2.165;倘若海水慢速結冰,水分子的原子氫氧鏈已規則性的排列在一直線上,水分子間已形成許多的空隙,因水慢速結冰,就有足夠的時間讓水分子把質量重密度大的鹽分子全部析出,沉澱在水下,不會包裹在冰晶的空隙裡形成鹽泡,而構成純淨的淡水冰,漂浮在水面上;同理,冰塊、碎冰、冰霜、冰水(液態冰),倘若溫度皆已達到海水的冰點以下,即-2℃以下,因水分子皆已規則性的排列,且皆已將質量重密度大的鹽分子全部析出,水分子間已膨脹鬆散,體積已大9%,皆同樣具備淡水冰的特質,漂浮在水面上。」 Regarding the operating principle of the first salt water separator, please refer to the explanation in Section [0004] of this manual: "After water freezes into ice, its volume increases by 9%": The water molecules in ice are formed by hydrogen chains, and their -O-H-O- atoms are arranged in a straight line. Due to this regular arrangement, many gaps are formed between the water molecules in ice; water molecules without hydrogen chains do not have this regular arrangement, and they will be stacked as tightly as possible (close packing). For example, the hydrogen chain bonding rate of water at room temperature is about 50%, while that of ice is 100% (the higher the hydrogen chain bonding rate of water, the more spaces between molecules), that is, ice is more regularly arranged than water, so the spaces between ice molecules are larger, so when the weight of water and ice is the same, the volume of ice is 9% larger; seawater is salt molecules and water molecules, combined in the state of a mixture, that is, combined in a physical state, and its structure is very fragile; water is composed of two elements, hydrogen and oxygen. The atomic mass of hydrogen is 1.00794u, which is the lightest element in the universe, and the atomic mass of oxygen is 15.9994, which is only second to hydrogen and helium, ranking third. The atomic mass of water is 17.00734; while salt, sodium chloride NaCl, is composed of two elements, chlorine and sodium. The atomic mass of chlorine is 35.45, and the atomic mass of sodium is 2.35. The mass of water is 22.9898, the atomic mass of salt is 58.4398, and the density of salt is 2.165. If seawater freezes slowly, the atomic hydrogen chains of water molecules are regularly arranged in a straight line, and many gaps have been formed between water molecules. Because water freezes slowly, there is enough time for water molecules to precipitate all the salt molecules with heavy mass and density and precipitate them underwater, instead of being wrapped in the gaps of ice crystals to form Salt bubbles form pure freshwater ice, which floats on the water. Similarly, ice cubes, crushed ice, frost, and ice water (liquid ice) all have the characteristics of freshwater ice and float on the water if the temperature has reached below the freezing point of seawater, that is, below -2°C, because the water molecules have been regularly arranged and all the salt molecules with high mass density have been precipitated, the water molecules have expanded and loosened, and the volume has increased by 9%. "
綜上所述,該第一鹽水分離機經過實際測試取得的資料,設定冰點以下適當的恆溫度數,讓該噴霧龍頭噴進來的水霧瞬間變成冰水;該葉片輪以適當的轉速,讓冰水保持液態冰的狀態持續流動;該旋轉桶以適當的轉速,產生適當的離心力、將已膨脹鬆散的水分子、礦物質和微量元素質量輕粒子細的分子,透過該半透膜適當的孔徑阻截篩選,甩出該旋轉桶外,儲存在該外殼桶裡;而鹽分子、礦物質和微量元素質量重粒子粗的分子,被該半透膜阻截留在該旋轉桶裡,而將鹽、水做適當的分離;倘生產出來的淡水未盡如人意,部分質量重粒子粗的礦物質和微量元素,仍感不足時,亦可從該鹵水儲存池所儲存的鹵水中萃取另行補充加入該淡水儲存池裡,使人類每天都可享用全方位營養豐富的天然自來水;按,礦物質是人體必需的元素,任何礦物質短缺,都會產生疾病,但人體卻無法自行產生或合成,必須由飲用水和食物中攝取,而唯有深層海水具備全方位所有的礦物質和微量元素,縱使不能由其分離出來的淡水中直接擷取,也 可由分離出來的鹵水中萃取補充加入該淡水儲存池裡,以維護人類的健康,改善人類的體質,延長人類的壽命。 In summary, the first salt water separator is set to an appropriate constant temperature below the freezing point based on the data obtained from actual tests, so that the water mist sprayed from the spray faucet instantly turns into ice water; the impeller rotates at an appropriate speed to keep the ice water in the state of liquid ice and continue to flow; the rotating barrel rotates at an appropriate speed to generate an appropriate centrifugal force to move the expanded and loosened water molecules The light and fine molecules of minerals and trace elements are blocked and screened by the appropriate pore size of the semipermeable membrane, thrown out of the rotating barrel and stored in the outer shell barrel; while the heavy and coarse molecules of salt molecules, minerals and trace elements are blocked by the semipermeable membrane and retained in the rotating barrel, and the salt and water are properly separated; if the fresh water produced is not satisfactory , some heavy and coarse minerals and trace elements are still insufficient, they can be extracted from the brine stored in the brine storage pool and added to the fresh water storage pool, so that humans can enjoy all-round nutritious natural tap water every day; according to, minerals are essential elements for the human body, any shortage of minerals will cause diseases, but the human body cannot produce or synthesize them by itself, and must be taken from drinking water and food. Only deep sea water has all-round minerals and trace elements. Even if they cannot be directly extracted from the separated fresh water, they can be extracted from the separated brine and added to the fresh water storage pool to maintain human health, improve human physique, and prolong human life.
所述第二鹽水分離機:係取消該第一鹽水分離機的下列設備:1、該旋轉桶的該半透膜。2、該旋轉桶的桶壁細孔。3、該第二馬達。4、該第二傳動齒輪;並增加下列設備:1、在該旋轉桶的上方開一個四方型的大孔,裝設一大型電動閘門。2、一第三馬達。3、一第三傳動齒輪;當該第二鹽水分離機的該冷凍壓縮機的開關打開,設定機內恆溫的適當度數,待機內的溫度達到恆溫的度數時,隨即打開該進水管的該進水電動閘門的開關,該噴霧龍頭即往下噴灑水霧開始進水,因深層海水的溫度本就維持在4℃~7℃左右的低溫,機內恆溫的度數設定在-2℃~-20℃海水冰點以下的度數,噴出的水霧機內的冷空氣很容易滲透進水霧中的小水滴裡,使小水滴快速降溫冷卻到冰點-2℃以下的度數,而變成冰水(液態冰);此時,該第二鹽水分離機的該第一馬達,帶動該第一傳動齒輪,轉動該葉片輪快速旋轉,使該噴霧龍頭噴進來的冰水跟著該葉片輪快速流動,冰水才不會瞬間結冰,維持液態冰的狀態持續流動;設該第二鹽水分離機的容量為3噸,且1分鐘灌滿3噸的海水,當海水灌滿時,該進水管的該進水電動閘門的開關隨即關閉,該葉片輪再持續旋轉10~20秒,確定水分子已全部變成冰水;該葉片輪的轉速隨即減速,形同煞車,使冰水的流速跟著減速,平穩地慢慢停下來;此時,冰水的水分子已膨脹鬆散,因水分子的質量最輕密度最小會浮在最上層,其他礦物質、微量元素、鹽分子,同樣在冰點-2℃以下的溫度,因此,所有元素的分子都非常安定,所有元素的分子會依照其本身的質量和密度的大 小,層次分明安定的沉澱在水分子的下面;經過實際測試,那些礦物質和微量元素要和水分子一起篩選隨同淡水一起取出,其停留在水下的高度位置在哪裡?根據該高度設定,迅速打開該第三馬達,帶動該第三傳動齒輪,依照設定的高度快速拉下該大型電動閘門,將浮在上層的淡水、礦物質、微量元素,排出該旋轉桶外,儲存在該外層外殼桶裡;當水分子、礦物質和微量元素質量輕密度小的分子,全部排出該旋轉桶外,儲存在該外層外殼桶底,隨即藉一淡水電動閘門把淡水輸水管的開關打開,將淡水全部輸送到所述淡水儲存池裡;此時,還留在該旋轉桶裡的鹵水,即鹽分子、礦物質和微量元素質量重密度大的分子,隨即藉一鹵水電動閘門把鹵水輸水管的開關打開,將鹵水全部輸送到所述鹵水儲存池裡,估計全部行程約2分鐘。 The second salt-water separator is a device that eliminates the following equipment of the first salt-water separator: 1. The semipermeable membrane of the rotary barrel. 2. The fine holes on the barrel wall of the rotary barrel. 3. The second motor. 4. The second transmission gear; and adds the following equipment: 1. A large square hole is opened on the top of the rotary barrel and a large electric gate is installed. 2. A third motor. 3. A third transmission gear; when the switch of the refrigeration compressor of the second salt water separator is turned on, the appropriate temperature of the machine is set, and when the temperature in the standby machine reaches the temperature, the switch of the water inlet electric gate of the water inlet pipe is immediately turned on, and the spray faucet sprays water mist downward to start water intake. Because the temperature of deep seawater is originally maintained at a low temperature of about 4℃~7℃, the temperature of the machine is set at -2℃~-20℃ below the freezing point of seawater. The cold air in the spray water mist machine can easily penetrate into the small water droplets in the water mist, causing the small water droplets to quickly cool down to a temperature below the freezing point of -2°C and become ice water (liquid ice). At this time, the first motor of the second salt water separator drives the first transmission gear to rotate the impeller wheel quickly, so that the ice water sprayed from the spray faucet flows quickly along with the impeller wheel, so that the ice water will not freeze instantly and maintain the state of liquid ice to continue to flow. Assume that the capacity of the second salt water separator is 3 tons, and it is filled with 3 tons of seawater in 1 minute. When the seawater is filled, the switch of the water inlet electric gate of the water inlet pipe is immediately closed, and the impeller continues to rotate for 10-20 seconds to make sure that all the water molecules have turned into ice water; the speed of the impeller is then decelerated, which is like a brake, so that the flow rate of the ice water is slowed down and slowly stops steadily; at this time, the water molecules in the ice water have expanded and loosened, because the mass of water molecules is the lightest and densest The lowest temperature will float to the top layer. Other minerals, trace elements, and salt molecules are also at a temperature below the freezing point of -2°C. Therefore, the molecules of all elements are very stable. The molecules of all elements will be clearly layered and steadily precipitated under the water molecules according to their own mass and density. After actual testing, those minerals and trace elements are screened together with water molecules and taken out together with fresh water. At what height do they stay underwater? According to the height setting, the third motor is quickly turned on to drive the third transmission gear, and the large electric gate is quickly pulled down according to the set height, so that the fresh water, minerals, and trace elements floating on the upper layer are discharged from the rotating barrel and stored in the outer shell barrel; when the water molecules, minerals, and trace elements with light mass and low density are all discharged from the rotating barrel and stored at the bottom of the outer shell barrel, Then, a fresh water electric gate is used to open the switch of the fresh water pipe, and all the fresh water is transported to the fresh water storage tank; at this time, the brine remaining in the rotating barrel, that is, the molecules with high mass density of salt molecules, minerals and trace elements, is immediately opened by a brine electric gate. The switch of the brine pipe is transported to the brine storage tank. The entire journey is estimated to take about 2 minutes.
同理,倘生產出來的淡水未盡如人意,部分質量重密度大的礦物質和微量元素,仍需補充加入淡水提供人類飲用,亦可從該鹵水儲存池所儲存的鹵水中萃取另行補充加入該淡水儲存池裡,使人類每天都可享用全方位營養豐富的天然自來水,以維護人類的健康,改善人類的體質,延長人類的壽命。 Similarly, if the fresh water produced is not satisfactory, some minerals and trace elements with high mass density still need to be added to the fresh water for human drinking. They can also be extracted from the brine stored in the brine storage tank and added to the fresh water storage tank, so that humans can enjoy all-round nutritious natural tap water every day to maintain human health, improve human physique, and prolong human life.
本發明另外公開一種〝深層海水淡化農業用水和工業用水大量生產系統〞,包括:一發電系統、一虹吸管機構、一抽水機構、一海水儲存池、至少二高壓重力沉澱池、一淡水儲存池,其中:所述發電系統、所述虹吸管機構、所述抽水機構、所述海水儲存池,所述淡水儲存池,皆和上述〝所述深層海水淡化民生用水大量生產系統〞的對應設備相同; 唯一不同的是,所述高壓重力沉澱池:因應農業用水和工業用水龐大的需求量,其容量依照淡水每日的需求量設置,倘日產需求量為270萬噸,則該高壓重力沉澱池的總容量既設為270萬噸,也就是,每個高壓重力沉澱池的容量設為90萬噸,即,長300米、寬100米、高30米;該高壓重力沉澱池設四個,使用三個日產量即為270萬噸,一個備用,每天輪流清洗一個,三天輪流清洗一次由備用支援;該高壓重力沉澱池的其他設備,皆和上述〝所述深層海水淡化民生用水大量生產系統〞的〝所述高壓重力沉澱池〞的設備相同。 The present invention also discloses a "deep seawater desalination agricultural water and industrial water mass production system", including: a power generation system, a siphon mechanism, a pumping mechanism, a seawater storage tank, at least two high-pressure gravity sedimentation tanks, and a freshwater storage tank, wherein: the power generation system, the siphon mechanism, the pumping mechanism, the seawater storage tank, and the freshwater storage tank are the same as the corresponding equipment of the above-mentioned "deep seawater desalination domestic water mass production system"; The only difference is that the capacity of the high-pressure gravity sedimentation tank: in response to the huge demand for agricultural and industrial water, is based on the fresh water per The daily demand is set. If the daily production demand is 2.7 million tons, the total capacity of the high-pressure gravity sedimentation tank is set to 2.7 million tons, that is, the capacity of each high-pressure gravity sedimentation tank is set to 900,000 tons, that is, 300 meters long, 100 meters wide, and 30 meters high; there are four high-pressure gravity sedimentation tanks, three of which have a daily production of 2.7 million tons, one is a spare, and one is cleaned in turn every day, and the spare is supported by the cleaning every three days; the other equipment of the high-pressure gravity sedimentation tank is the same as the equipment of the "high-pressure gravity sedimentation tank" in the above-mentioned "deep seawater desalination and domestic water mass production system".
由於深層海水本已相當潔淨,經過該高壓重力沉澱池的高壓重力沉澱後已更加潔淨,只要藉該半透膜隔離板及該半透膜隔離管把質量最重粒子最粗的鹽分子,隨同重金屬、硬度雜質、和化學殘留物質一起隔離排除後,剩下的淡水、礦物質、微量元素,既營養又肥沃,全部做為農業用水和工業用水使用,安全已無慮,是故,省略該第一鹽水分離機及該第二鹽水分離機的冷凍分離程序,直接將過濾出來的淡水輸入該淡水儲存池裡,讓低溫的海淡水,普灑大地,降低土壤溫度,改善土質,使大地遍地變成黑土,廣增糧食,拓展畜牧,造林植被,治理沙漠,以解決糧食不足危機,水質源匱乏危機,地球暖化危機,而維護動植物的生存環境。 Since deep seawater is already quite clean, it becomes even cleaner after high-pressure gravity sedimentation in the high-pressure gravity sedimentation tank. As long as the heaviest and coarsest salt molecules are separated and removed together with heavy metals, hard impurities, and chemical residues by the semipermeable membrane isolation plate and the semipermeable membrane isolation tube, the remaining fresh water, minerals, and trace elements are both nutritious and fertile, and can all be used as agricultural and industrial water without any safety concerns. , omitting the freezing separation process of the first salt water separator and the second salt water separator, directly inputting the filtered fresh water into the fresh water storage tank, allowing the low-temperature sea water to sprinkle on the earth, lower the soil temperature, improve the soil quality, turn the earth into black soil, increase food, expand animal husbandry, plant forests, and control deserts, so as to solve the food shortage crisis, water quality source shortage crisis, global warming crisis, and maintain the living environment of animals and plants.
本發明另外公開一種〝表層海水淡化大量生產系統〞,包括:一海水儲存池、至少二高壓重力沉澱池、一淡水儲存池,其中:所述海水儲存池,所述高壓重力沉澱池、所述淡水儲存池,皆和上述〝所述深層海水淡化農業用水和工業用水大量生產系統〞的對應設備相同。 The present invention also discloses a "surface seawater desalination mass production system", including: a seawater storage tank, at least two high-pressure gravity sedimentation tanks, and a freshwater storage tank, wherein: the seawater storage tank, the high-pressure gravity sedimentation tank, and the freshwater storage tank are the same as the corresponding equipment of the above-mentioned "deep seawater desalination agricultural water and industrial water mass production system".
本發明另外公開一種〝第一鹽水分離機〞:該第一鹽水分離機和上述〝所述深層海水淡化民生用水大量生產系統〞的〝所述第一鹽水分離機〞的設備相同,可單獨作為表層海水淡化小量生產使用。 The present invention also discloses a "first salt water separator": the first salt water separator has the same equipment as the "first salt water separator" of the above-mentioned "deep seawater desalination and domestic water mass production system", and can be used alone for small-scale production of surface seawater desalination.
本發明另外公開一種〝第二鹽水分離機〞:該第二鹽水分離機和上述〝所述深層海水淡化民生用水大量生產系統〞的〝所述第二鹽水分離機〞的設備相同,可單獨作為表層海水淡化小量生產使用。 The present invention also discloses a "second salt water separator": the second salt water separator has the same equipment as the "second salt water separator" of the above-mentioned "deep seawater desalination and domestic water mass production system", and can be used alone for small-scale production of surface seawater desalination.
茲為使 貴審查委員對本發明產品的技術特徵及所達成的功效,有更進一步的了解與認識,謹佐以較佳的實施例圖,按圖再度逐一詳加闡述如後: In order to enable the review committee to have a deeper understanding and knowledge of the technical features and effects achieved by the product of this invention, we would like to provide a better implementation diagram and further explain it one by one according to the diagram as follows:
1:發電系統 1: Power generation system
2:虹吸管機構 2: Siphon mechanism
21:固定座 21: Fixed seat
3:海水儲存池 3: Seawater storage tank
31:輸水管 31: Water pipes
32:抽水機 32: Pump
33:進水電動閘門 33: Water inlet electric gate
34:出水電動閘門 34: Water outlet electric gate
4:高壓重力沉澱池 4: High-pressure gravity sedimentation tank
4A:第一高壓重力沉澱池 4A: The first high-pressure gravity sedimentation tank
4B:第二高壓重力沉澱池 4B: Second high-pressure gravity sedimentation tank
4C:第三高壓重力沉澱池 4C: The third high-pressure gravity sedimentation tank
A1:第一下池 A1: First time in the pool
B1:第二下池 B1: Second pool
C1:第三下池 C1: The third time in the pool
A2:第一上池 A2: First upper pool
B2:第二上池 B2: Second upper pool
C2:第三上池 C2: The third upper pool
41:輸水管 41: Water pipe
42:海水排水管 42: Seawater drainage pipe
43:抽水機 43: Pump
44;半透膜隔離管 44; Semipermeable membrane isolation tube
45:進水電動閘門 45: Water inlet electric gate
46:半透膜隔離板 46: Semipermeable membrane separator
47:排水電動閘門 47: Drainage electric gate
5A:第一鹽水分離機 5A: First salt water separator
511:進水管 511: Water inlet pipe
512:進水電動閘門 512: Water inlet electric gate
51:淡水輸水管 51: Fresh water pipeline
52:鹵水輸水管 52:Brine pipe
53:噴霧龍頭 53: Spray faucet
54:葉片輪 54: Impeller
55:半透膜 55: Semipermeable membrane
56:旋轉桶 56: Rotating barrel
57:軸承 57: Bearings
572A:第一馬達 572A: First Motor
572B:第二馬達 572B: Second Motor
571A:第一傳動齒輪 571A: First drive gear
571B:第二傳動齒輪 571B: Second transmission gear
58:冷凍壓縮機 58: Freeze compressor
591:淡水電動閘門 591: Freshwater electric gate
592:鹵水電動閘門 592: Halogen electric gate
5B:第二鹽水分離機 5B: Second salt water separator
59:大型電動閘門 59: Large electric gate
581:第三馬達 581: The third motor
582:第三傳動齒輪 582: Third transmission gear
6:淡水儲存池 6: Fresh water storage tank
61:淡水第一輸出管 61: Fresh water first output pipe
62:淡水第二輸出管 62: Fresh water second output pipe
63:半透膜清洗管 63: Semipermeable membrane cleaning tube
64:清洗電動閘門 64: Cleaning the electric gate
7:鹵水儲存池 7:Brine storage tank
71:鹵水輸出管 71:Brine output pipe
圖1為本發明「深層海水淡化民生用水大量生產系統」整體系統的立體結構示意圖;圖2為本發明海水儲存池、高壓重力沉澱池的整體系統示意圖;圖3為本發明海水儲存池、高壓重力沉澱池的側面系統示意圖;圖4為本發明第一鹽水分離機的整體結構示意圖;圖5為本發明第一鹽水分離機的側面結構示意圖;圖6為本發明第二鹽水分離機的整體結構示意圖;圖7為本發明第二鹽水分離機的側面結構示意圖;圖8為本發明「深層海水淡化農業用水和工業用水大量生產系統」整體系統的立體結構示意圖;圖9為本發明海水儲存池、高壓重力沉澱池的整體系統結構示意圖; 圖10為本發明海水儲存池、高壓重力沉澱池的側面部分結構示意圖;圖11為本發明第一鹽水分離機獨立使用的結構示意圖;圖12為本發明第一鹽水分離機獨立使用的側面結構示意圖。 FIG1 is a three-dimensional structural diagram of the overall system of the "deep seawater desalination system for domestic water mass production" of the present invention; FIG2 is a schematic diagram of the overall system of the seawater storage tank and the high-pressure gravity sedimentation tank of the present invention; FIG3 is a side system schematic diagram of the seawater storage tank and the high-pressure gravity sedimentation tank of the present invention; FIG4 is a schematic diagram of the overall structure of the first salt water separator of the present invention; FIG5 is a schematic diagram of the side structure of the first salt water separator of the present invention; FIG6 is a schematic diagram of the overall structure of the second salt water separator of the present invention; FIG7 is a schematic diagram of the second salt water separator of the present invention Figure 8 is a schematic diagram of the side structure of the separator; Figure 8 is a three-dimensional schematic diagram of the overall system of the "deep seawater desalination agricultural water and industrial water mass production system" of the present invention; Figure 9 is a schematic diagram of the overall system structure of the seawater storage tank and high-pressure gravity sedimentation tank of the present invention; Figure 10 is a schematic diagram of the side structure of the seawater storage tank and high-pressure gravity sedimentation tank of the present invention; Figure 11 is a schematic diagram of the structure of the first salt water separator of the present invention when used independently; Figure 12 is a schematic diagram of the side structure of the first salt water separator of the present invention when used independently.
以下結合附圖1~12,進一步說明本發明〝深層海水淡化民生用水大量生產系統及部件〞的具體實施方式。本發明深層海水淡化民生用水大量生產系統及部件不限於以下實施例的描述。 The following is combined with Figures 1 to 12 to further illustrate the specific implementation of the "deep seawater desalination system and components for mass production of domestic water" of the present invention. The deep seawater desalination system and components for mass production of domestic water of the present invention are not limited to the description of the following embodiments.
實施例1:Embodiment 1:
本實施例給出〝深層海水淡化民生用水大量生產系統〞的具體實施方式,如圖1~圖7所示,包括:一發電系統1、一虹吸管機構2、一抽水機構(圖中未示)、一海水儲存池3、至少二高壓重力沉澱池4、至少二第一鹽水分離機5A/或至少二第二鹽水分離機5B、一淡水儲存池6、一鹵水儲存池7,其中:所述發電系統1:係發明人所發明的「海浪浮力和地心引力發電系統」,貴局於2020年5月1日核准發明第I692580號,做為本深層海水淡化民生用水大量生產系統的電源設備,有效解決耗能大、成本高、大量生產所面臨的成本問題。
This embodiment provides a specific implementation method of the "deep seawater desalination and domestic water mass production system", as shown in Figures 1 to 7, including: a
所述虹吸管機構2:如圖1所示,係藉該虹吸管機構2的虹吸原理,長臂虹吸管往下延伸600米直接深入深層的海裡,往上再延伸跨越所述海水儲存池3的牆壁頂端才轉彎,短臂虹吸管則往下延伸到該海水儲存池3底;倘短臂虹吸管管內的液面,比長臂虹吸管管內的液面為低時,則,當虹吸管藉抽水機構的一抽水機,將水抽入該海水儲存池3裡,整條
虹吸管已灌滿海水後,虹吸作用已成立,隨即關掉該抽水機,深層海水仍然會經由虹吸管繼續流到該海水儲存池3裡,不會停止流動;倘短臂虹吸管管內的液面,比長臂虹吸管管內的液面為高時,則,該海水儲存池3裡的海水將會倒流回深層的海裡;此時,必須藉助該抽水機構的抽水機將深層海水抽入該海水儲存池3裡。
The siphon mechanism 2: As shown in FIG1, the siphon
所述抽水機構(圖中未示):係應用該抽水機構的抽水機,補強該虹吸管機構2的虹吸作用力不足時使用;即,在該虹吸管機構2的短臂虹吸管管內的液面,比長臂虹吸管管內的液面高,無法藉助虹吸作用力將水抽入該海水儲存池3時,得啟動該抽水機構的抽水機,將水抽入該海水儲存池3裡;也就是,利用該虹吸管機構2的虹吸作用力,節省該抽水機構的抽水機能源的消耗量,而達節能的效果。
The pumping mechanism (not shown in the figure) is a pumping machine of the pumping mechanism, which is used to supplement the insufficient siphon force of the siphon
所述海水儲存池3:如圖1~圖3所示,長度與所述高壓重力沉澱池4相同,然容量必須比該高壓重力沉澱池4的容量大;由於重量太大,為確保結構安全,該海水儲存池3必須部分深入地下,以策安全;該海水儲存池3的底部設多根大口徑的輸水管31,直通該高壓重力沉澱池4的底部;每根輸水管31的進水口設一進水電動閘門33,一抽水機32,可快速將該高壓重力沉澱池4灌滿。
The seawater storage tank 3: As shown in Figures 1 to 3, the length is the same as that of the high-pressure
所述高壓重力沉澱池4:至少設二個,即,第一高壓重力沉澱池4A/及第二高壓重力沉澱池4B;如圖1~圖3所示,其容量依照淡水每日的需求量設置,倘日產需求量為45萬噸,則該第一高壓重力沉澱池4A/及該第二高壓重力沉澱池4B的容量既設為45萬噸,即,長300米、寬50米、高30米;在該第一高壓重力沉澱池4A/及該第二高壓重力沉澱池4B的
高20米處,設一半透膜隔離板46,將該第一高壓重力沉澱池4A/及該第二高壓重力沉澱池4B分隔成:第一下池A1/及第二下池B1、第一上池A2/及第二上池B2;該第一下池A1/及該第二下池B1:如圖3所示,係由該半透膜隔離板46到該第一高壓重力沉澱池4A/及該第二高壓重力沉澱池4B的底部所構成,即水深10米~30米的範圍;此部分,水的重力壓強P=2大氣壓P0~4大氣壓P0,在此一高壓重力的環境下進行沉澱,讓有毒的重金屬、硬度雜質、化學殘留物質等受地心引力的影響快速沉澱,倘這些質量重粒子粗的重金屬、硬度雜質、化學殘留物質,違反自然法則,往上攀升穿越該半透膜隔離板46時,因該半透膜隔離板46位於水深10米處,其下壓力=側壓力=上壓力=2大氣壓P0,將會以2大氣壓P0的下壓力協助該半透膜隔離板46從上把它擋住、也會以2大氣壓P0的側壓力協助該半透膜隔離板46從旁把它推走、再加上這些物質本身的重力受地心引力往下拉、以及該半透膜隔離板46奈米級的孔徑阻截,質量重粒子粗的重金屬、硬度雜質、化學殘存物質,實難往上攀升硬闖穿越該半透膜隔離板46而成漏網之魚,進入該第一上池A2/及該第二上池B2裡;該第一下池A1/及該第二下池B1的底部由該海水儲存池3直接延伸過來的多根輸水管31往下轉彎,出口處分別設一出水電動閘門34;該第一高壓重力沉澱池4A/及該第二高壓重力沉澱池4B的底部外側,分別設一排水電動閘門47、一海水排水管42直通海裡;該第一上池A2/及該第二上池B2:如圖3所示,係由該半透膜隔離板46到該第一高壓重力沉澱池4A/及該第二高壓重力沉澱池4B的
頂部所構成,即水面~水深10米的範圍;此部分,設多根大口徑的輸水管41,每根輸水管41的進水口設一進水電動閘門45、一半透膜隔離管44、一抽水機43;該第一上池A2/及該第二上池B2的出水總流量等於該第一下池A1/及該第二下池B1的進水總流量,使該第一高壓重力沉澱池4A/及該第二高壓重力沉澱池4B的水位始終保持不變;該半透膜隔離管44的半透膜和該半透膜隔離板46的半透膜一樣,僅過濾有毒的重金屬、硬度雜質、化學殘留物質外,鹽分、礦物質和微量元素將全部讓其通過,送給所述第一鹽水分離機5A/或所述第二鹽水分離機5B,進行鹽、水、礦物質和微量元素等的分離;如圖1~圖3所示,該第一高壓重力沉澱池4A/及該第二高壓重力沉澱池4B;必須二個一起灌滿後,才可開始使用;每天使用一個,另一個清洗乾淨重灌沉澱一天後,隔天才使用;也就是,今天使用新池,昨天已用過的舊池,將該舊池底部外側的該海水排水管42的該排水電動閘門47的開關打開,把該舊池的水全部經由該海水排水管42直接排入海裡;當該舊池往下不斷排水,該第一下池A1/或該第二下池B1的水將很快排光,該第一上池A2/或該第二上池B2乾淨的水自然垂直往下流,水重力自然全部往下壓快速沖刷清洗該半透膜隔離板46,緊接著再把該第一下池A1/或該第二下池B1也沖刷清洗乾淨;此時,所述淡水儲存池6,設一半透膜清洗管63、一清洗電動閘門64;該半透膜清洗管63從該淡水儲存池6連接到該第一上池A2/及該第二上池B2的每根該半透膜隔離管44的上面,隨即打開該半透膜清洗管63的該清洗電動閘門64的開關,開始往下噴水快速沖洗該半透膜隔離管44;待該半透膜隔離管44、該半透膜隔離板46、
該第一下池A1/或該第二下池B1,全部沖刷清洗乾淨,把水排光;才關閉該海水排水管42的該排水電動閘門47的開關,開始重新進水將該舊池灌滿;兩個高壓重力沉澱池4,周而復始,來回更換,每天都把該半透膜隔離管44、該半透膜隔離板46、該第一下池A1/及該第二下池B1,全部沖刷清洗乾淨,才重新灌水使用,因此,該半透膜隔離管44、該半透膜隔離板46,該第一下池A1/及該第二下池B1,可以確保乾淨,不會造成阻塞,以維護系統通暢順利運行。
The high-pressure
根據經濟部水利產業資訊網公布:深層海水優越性的五大特質,請參考本說明書【0016】節說明:「1、清澈乾淨性:人為的污染不易到達,是構成深層海水潔淨的原因之一。另外,表層海水在沉澱過程中,細菌會因化學酸化、沉澱、漂流擴散等之分解作用,隨深度而逐漸減少,且因深海缺少殘存的有機物質及硝酸體氮素等細菌所需的養份,細菌難以生存繁殖。因此,導致動植物病變的各種有害細菌或病毒,在深層海水中的含量均極為稀少,僅為表層海水的千分之一至萬分之一。再者,殘存於深層海水的有機物,對微生物分解殘渣有機物作用的抵抗性相當安定,這也是深層海水的水質在微生物學或物理化學方面較為安定、無機且清淨的原因。」 According to the Ministry of Economic Affairs' Water Conservancy Industry Information Network, there are five major characteristics of deep seawater. Please refer to the explanation in Section [0016] of this manual: "1. Clarity and cleanliness: It is difficult for artificial pollution to reach deep seawater, which is one of the reasons why deep seawater is clean. In addition, during the sedimentation process of surface seawater, bacteria will gradually decrease with depth due to decomposition such as chemical acidification, sedimentation, drift diffusion, etc., and because the deep sea lacks residual organic matter and nitrate nitrogen, etc. The nutrients required by bacteria make it difficult for them to survive and reproduce. Therefore, the content of various harmful bacteria or viruses that cause animal and plant diseases in deep seawater is extremely rare, only one thousandth to one ten-thousandth of that in surface seawater. Furthermore, the organic matter remaining in deep seawater is quite resistant to the decomposition of residual organic matter by microorganisms, which is why the water quality of deep seawater is relatively stable, inorganic and clean in terms of microbiology or physical chemistry. ”
綜上所述,深層海水本已相當乾淨,縱使還有少量的殘存重金屬、硬度雜質,或化學殘留物質,也可藉該高壓重力沉澱池4以高壓重力的方式快速沉澱,並藉該半透膜隔離板46及該半透膜隔離管44奈米級的孔徑阻截而加以排除。
In summary, deep seawater is already quite clean. Even if there are still a small amount of residual heavy metals, hard impurities, or chemical residues, they can be quickly precipitated by high-pressure gravity in the high-pressure
由於現有表層海水淡化系統使用逆滲透RO膜分離淡水與
鹵水,連同極其珍貴的礦物質及微量元素也一併排除,致生產出來的淡水已無營養,頗為可惜;因此,該半透膜隔離板46及該半透膜隔離管44所使用的半透膜,其孔徑不宜太微細,除可排除重金屬、硬度雜質、化學殘留物質等質量重粒子粗的有毒物質外,深層海水所含豐厚的礦物質包括:鎂、鈣、鉀等,及微量元素包含:鋅、銅、硼、磷、硒等八十多種元素,皆已和水分子及鹽分子,常年處於低溫高壓的深層海裡,分子結構已偏小、穩定,分子間已不易重組結合,極具穩定與微小之分子結構特性(請參考:本說明書第【0017】、【0018】、【0019】、【0020】各節的說明既明);因此必須保存這些珍貴的營養品穿越該半透膜隔離板46及該半透膜隔離管44進入該第一鹽水分離機裡,不能將其排除;目前半透膜的成品較適合的有:1、RO膜(reverse osmosis):透水孔徑0.0001~0.002micron。2、NF膜(nanofiltration):透水孔徑0.0009~0.009micron;3、UF膜(ultrafiltration):透水孔徑0.006~0.11micron;4、MF膜(microfiltration):透水孔徑0.08~1.2micron;還有很多,謹摘錄較適合的部分提供參考。在所有半透膜的項目中唯有逆滲透RO膜的透水孔徑最小,在0.0001~0.002micron之間,如以人體頭髮做比較,人體頭髮之外徑約為10micron,即可知逆滲透RO膜孔徑之精密;然該高壓重力沉澱池4的目的,僅作為排除深層海水極微少質量重粒子粗的重金屬、硬度雜質、和化學殘留物質,故採用透水孔徑較粗的第3項UF膜透水孔徑0.006~0.11micron,或第4項MF膜透水孔徑0.08~1.2micron,才能保存這些珍貴的營養品。
Since the existing surface seawater desalination system uses reverse osmosis RO membrane to separate fresh water and brine, extremely precious minerals and trace elements are also removed, resulting in the fresh water produced having no nutrients, which is a pity; therefore, the semipermeable membrane used in the semipermeable
所述第一鹽水分離機5A:如圖4、圖5所示,設內外兩層外殼,該外層外殼:設一層保溫膜(圖中未示)、一冷凍壓縮機58、一溫度控
制器(圖中未示);該保溫膜:可隔絕外面的溫度,保持機內的溫度恆溫;該冷凍壓縮機58:可提供冷氣維持機內-2℃~-20℃的恆溫環境;該溫度控制器:可隨意設定機內的恆溫度數;如圖4、圖5所示,該內層外殼:設一旋轉桶56,該旋轉桶56由一第二馬達572B,帶動一第二傳動齒輪571B,轉動該旋轉桶56旋轉;該旋轉桶56的桶壁設許多細密的小孔,其內層的桶壁緊貼一層半透膜55,水分子、礦物質和微量元素質量輕粒子細的分子,可透過該半透膜55由桶壁的細孔外溢;鹽分子、礦物質和微量元素質量重粒子粗的分子,無法透過該半透膜55外溢;該旋轉桶56的中心設一葉片輪54,該葉片輪54的上下設兩個軸承57以固定該葉片輪54,幫助該葉片輪54穩定旋轉;該葉片輪54由一第一馬達572A,帶動一第一傳動齒輪571A,轉動該葉片輪54旋轉;如圖4、圖5所示,該第一鹽水分離機5A設一進水管511,該進水管511設一進水電動閘門512、一噴霧龍頭53;該噴霧龍頭53,可將海水調成噴霧狀,往下噴灑進水;當該進水管511的該進水電動閘門512的開關打開,該噴霧龍頭53將水調成噴霧狀往下噴灑進水時,因深層海水的溫度本就維持在4℃~7℃左右的低溫,機內恆溫的度數設定在-2℃~-20℃海水冰點以下的度數,噴出的水霧機內的冷空氣很容易滲透進水霧中的小水滴裡,使小水滴快速降溫冷卻到冰點-2℃以下的度數,而變成冰水(液態冰);當該噴霧龍頭53開始噴出水霧進水時,該第一鹽水分離機5A的該第一馬達572A,帶動該第一傳動齒輪571A,轉動該葉片輪54快速旋轉,使該噴霧龍頭53噴進來的冰水跟著該葉片輪54快速流動,冰水才不會瞬間
結冰,維持液態冰的狀態持續流動;設該第一鹽水分離機5A的容量為3噸,且1分鐘灌滿3噸的海水,當海水灌滿時,該進水管511的該進水電動閘門512的開關隨即關閉,該葉片輪54再持續旋轉10~20秒,確定水分子已全部變成冰水;此時,該第二馬達572B,帶動該第二傳動齒輪571B,轉動該旋轉桶56快速旋轉,將水分子已膨脹鬆散的冰水,藉該旋轉桶56的離心力將水分子、礦物質和微量元素質量輕粒子細的分子,甩出該旋轉桶56的外層外殼桶裡;而鹽分子、礦物質和微量元素質量重粒子粗的分子,被該旋轉桶56的該半透膜55阻截而留在該旋轉桶56裡;如圖4、圖5所示,當水分子、礦物質和微量元素質量輕粒子細的分子,全部甩出該旋轉桶56外,儲存在該外層外殼桶底後,隨即藉一淡水電動閘門591把淡水輸水管51的開關打開,將淡水全部輸送到所述淡水儲存池6裡;此時,儲存在該旋轉桶56裡的鹵水,即鹽分子、礦物質和微量元素質量重粒子粗的分子,隨即藉一鹵水電動閘門592把鹵水輸水管52的開關打開,將鹵水全部輸送到所述鹵水儲存池7裡,估計全部行程約2分鐘。
The first
如圖1所示,該第一鹽水分離機5A的裝設排數和台數,係依照淡水每天的需求量設置;倘該第一鹽水分離機5A每台的容量設為3噸,2分鐘輸出一次,即每分鐘的生產量為1.5噸;則,配合該高壓重力沉澱池4日產量設為45萬噸計算:需安裝:450000噸÷24時÷60分÷1.5噸/分=209台,則,設11排,每排21台,共安裝231台,多安裝了1排21台,係每天逐排停機一次,沖刷清洗該第一鹽水分離機5A的該半透膜55,避免
阻塞影響生產出來的淡水品質;如圖1所示,該高壓重力沉澱池4配合該第一鹽水分離機5A的裝設排數,設11根大口徑的輸水管41,直接穿越該11排的該第一鹽水分離機5A的上面,使用三向接頭往下與該第一鹽水分離機5A的該進水管511連接;如圖4、圖5所示,該進水管511的該噴霧龍頭53,亦可調整改變噴水的模式噴出水刀,該第一鹽水分離機5A每天逐排停機一次,該噴霧龍頭53朝下方的四周噴出水刀,沖刷清洗機內的該半透膜55,以免阻塞,影響生產出來的淡水品質。
As shown in FIG1 , the number of rows and units of the first
有關該第一鹽水分離機5A的操作原理,請參考本說明書節的說明既明:「〝水結成冰後,體積增加9%〞:冰的水分子是由氫氧鏈結合而成,其-O-H-O-原子排列在一直線上,由於這個規則性的排列關係,冰的水分子間形成許多的空隙;而沒有氫鏈結合的水分子,就沒有這種規則性的排列,它會盡量的緊密堆積在一起(close packing)。如室溫的水,其氫鏈結合率約為50%,而冰為100%(氫鏈結合比率越高的水,分子間的空隙就越多),也就是,冰較水規則性的排列高,所以冰的分子間空隙大,因此水和冰的重量相同時,冰的體積大9%;而海水乃是鹽分子和水分子,以混合物的狀態相結合,也就是,以物理狀態結合,其結構非常脆弱;而水是由氫、氧兩種元素組成,氫原子質量為1.00794u,是宇宙最輕的元素,氧原子質量為15.9994,僅次於氫和氦,佔第三位,水的原子質量為17.00734;而鹽,氯化鈉NaCl,是由氯、鈉兩種元素組成,氯原子質量為35.45,鈉原子質量為22.9898,鹽的原子質量為58.4398,鹽的密度為2.165;
倘若海水慢速結冰,水分子的原子氫氧鏈已規則性的排列在一直線上,水分子間已形成許多的空隙,因水慢速結冰,就有足夠的時間讓水分子把質量重密度大的鹽分子全部析出,沉澱在水下,不會包裹在冰晶的空隙裡形成鹽泡,而構成純淨的淡水冰,漂浮在水面上;同理,冰塊、碎冰、冰霜、冰水(液態冰),倘若溫度皆已達到海水的冰點以下,即-2℃以下,因水分子皆已規則性的排列,且皆已將質量重密度大的鹽分子全部析出,水分子間已膨脹鬆散,體積已大9%,皆同樣具備淡水冰的特質,漂浮在水面上。」
Regarding the operating principle of the first
綜上所述,該第一鹽水分離機5A透過實際測試取得的資料,設定冰點以下適當的恆溫度數,讓該噴霧龍頭53噴進來的水霧瞬間變成冰水;該葉片輪54以適當的轉速,讓冰水保持液態冰的狀態持續流動;該旋轉桶56以適當的轉速,產生適當的離心力、將已膨脹鬆散的水分子、礦物質和微量元素質量輕粒子細的分子,透過該半透膜55適當的孔徑篩選,甩出該旋轉桶56外,儲存在該外殼的桶裡;而鹽分子、礦物質和微量元素質量重粒子粗的分子,被該半透膜55阻截留在該旋轉桶56裡,而將鹽、水做適當的分離;倘生產出來的淡水未盡如人意,部分質量重粒子粗的礦物質和微量元素,仍然不足時,亦可從該鹵水儲存池7所儲存的鹵水中萃取另行補充加入該淡水儲存池6,使人類每天都可享用全方位營養豐富的天然自來水;按,礦物質是人體必需的元素,任何礦物質短缺,都會產生疾病,但人體卻無法自行產生或合成,必須由飲用水和食物中攝取,而唯有深層海水具備全方位所有的礦物質和微量元素,且其存量非常豐富,縱使不能由分離出來的淡水中直接擷取,也可由分離出來的鹵水中萃取另行補充加入該淡水儲存池6裡,以維護人類的健康,改善人類的體質,延長人
類的壽命。
In summary, the first
所述第二鹽水分離機5B:如第4~7圖所示,係取消該第一鹽水分離機5A的下列設備:1、該旋轉桶56的該半透膜55。2、該旋轉桶56的桶壁細孔。3、該第二馬達572B。4、該第二傳動齒輪571B;並增加下列設備:1、在該旋轉桶56的上方開一個四方型的大孔,裝設一大型電動閘門59。2、一第三馬達581。3、一第三傳動齒輪582;如圖6、圖7所示,當該第二鹽水分離機5B的該冷凍壓縮機58的開關打開,設定機內恆溫的適當度數,待機內的溫度達到恆溫的度數時,隨即打開該進水管511的該進水電動閘門512的開關,該噴霧龍頭53即往下噴灑水霧開始進水,因深層海水的溫度本就維持在4℃~7℃左右的低溫,機內恆溫的度數設定在-2℃~-20℃的海水冰點以下的度數,噴出的水霧機內的冷空氣很容易滲透進水霧中的小水滴裡,使小水滴快速降溫冷卻到冰點-2℃以下的度數,而變成冰水(液態冰);此時,該第一馬達572A,帶動該第一傳動齒輪571A,轉動該葉片輪54快速旋轉,使該噴霧龍頭53噴進來的冰水跟著該葉片輪54快速流動,冰水才不會瞬間結冰,維持液態冰的狀態持續流動;設該第二鹽水分離機5B的容量為3噸,且1分鐘灌滿3噸的海水,當海水灌滿時,該進水管511的該進水電動閘門512的開關隨即關閉,該葉片輪54再持續旋轉10~20秒,確定水分子已全部變成冰水;該葉片輪54的轉速隨即減速,形同煞車,使冰水的流速跟著減速,平穩地停下來;此時,冰水的水分子已膨脹鬆散,因水分子的質量最輕密度最小會浮在最上層,其他礦物質、微量元素、鹽分子,同樣在冰點-2℃以下相同的
溫度,因此,所有元素的分子都非常安定,所有元素的分子會依照其本身的質量和密度的大小,層次分明安定的沉澱在水分子的下面;經過實際測試,那些礦物質和微量元素要和水分子一起篩選隨同淡水一起取出,其停留在水中的高度位置在哪裡?根據該高度設定,迅速打開該第三馬達581,帶動該第三傳動齒輪582,依照設定的高度拉下該大型電動閘門59,將浮在上層的淡水、礦物質、微量元素,排出該旋轉桶56,儲存在該外層外殼桶裡;如圖6、圖7所示,當水分子、礦物質和微量元素質量輕密度小的分子,全部排出該旋轉桶56外,儲存在該外層外殼桶底後,隨即藉一淡水電動閘門591把淡水輸水管51的開關打開,將淡水全部輸送到所述淡水儲存池6裡;此時,儲存在該旋轉桶56裡的鹵水,即鹽分子、礦物質和微量元素質量重密度大的分子,隨即藉一鹵水電動閘門592把鹵水輸水管52的開關打開,將鹵水全部輸送到所述鹵水儲存池7裡,估計全部行程約2分鐘。
The second salt-
同理,倘生產出來的淡水未盡如人意,部分質量重密度大的礦物質和微量元素,仍需補充加入淡水提供人類飲用,亦可從該鹵水儲存池7所儲存的鹵水中萃取另行補充加入該淡水儲存池6裡,使人類每天都可享用全方位營養豐富的天然自來水,以維護人類的健康,改善人類的體質,延長人類的壽命。
Similarly, if the produced fresh water is not satisfactory, some minerals and trace elements with high mass density still need to be added to the fresh water for human drinking. They can also be extracted from the brine stored in the
實施例2:Embodiment 2:
本實施例給出另外一種〝深層海水淡化農業用水和工業用水大量生產系統〞的具體實施方式,如圖8~圖10所示,包括:一發電系統
1、一虹吸管機構2、一抽水機構(圖中未示)、一海水儲存池3、至少二高壓重力沉澱池4、一淡水儲存池6,其中:所述發電系統1、所述虹吸管機構2、所述抽水機構、所述海水儲存池3,所述淡水儲存池6,如圖8~圖10所示,皆和上述實施例1的〝所述深層海水淡化民生用水大量生產系統〞的對應設備相同;如圖8~圖10所示,唯一不同的是,所述高壓重力沉澱池4:因應農業用水和工業用水龐大的需求量,其容量依照淡水每日的需求量設置,倘日產需求量為270萬噸,則該高壓重力沉澱池4的總容量既設為270萬噸,也就是,每個高壓重力沉澱池4的容量設為90萬噸,即,長300米、寬100米、高30米;該高壓重力沉澱池4設四個,使用三個,即,第一高壓重力沉澱池4A/及第二高壓重力沉澱池4B/及第三高壓重力沉澱池4C,三個高壓重力沉澱池4日產量既為270萬噸,一個備用(圖中未示),每天輪流清洗一個,三天輪流清洗一次由備用支援;該高壓重力沉澱池4的其他設備,如圖8~圖10所示,皆和上述實施例1的〝所述深層海水淡化民生用水大量生產系統〞的〝所述高壓重力沉澱池4〞的設備相同。
This embodiment provides another specific implementation method of "deep seawater desalination agricultural water and industrial water mass production system", as shown in Figures 8 to 10, including: a
由於深層海水本已相當潔淨,經過該高壓重力沉澱池4的高壓重力沉澱後已更加潔淨,只要將該半透膜隔離板46及該半透膜隔離管44的半透膜孔徑略為加細,能夠將質量最重粒子最粗的鹽分子、隨同重金屬、硬度雜質、化學殘留物質一起隔離排除,既可將飽含礦物質和微量元素既營養又肥沃的海淡水全部做為農業用水和工業用水使用,安全已無慮,是故,省略該第一鹽水分離機5A,及該第二鹽水分離機5B的冷凍分離程序,
直接將過濾出來的淡水輸入該淡水儲存池6裡,讓低溫的海淡水,普灑大地,降低土壤溫度,改善土質,使大地遍地變成黑土,廣增糧食,拓展畜牧,造林植被,治理沙漠,以解決糧食不足危機,水質源匱乏危機,地球暖化危機,而維護動植物的生存環境。
Since deep seawater is already quite clean, it becomes even cleaner after high-pressure gravity sedimentation in the high-pressure
實施例3:Embodiment 3:
本實施例給出另外一種〝表層海水淡化大量生產系統〞的具體實施方式,如圖8~圖10所示,包括:一海水儲存池3、至少二高壓重力沉澱池4、一淡水儲存池6,其中:所述海水儲存池3,所述高壓重力沉澱池4、所述淡水儲存池6,如圖8~圖10所示,皆和上述實施例2的〝所述深層海水淡化農業用水和工業用水大量生產系統〞的對應設備相同。
This embodiment provides another specific implementation method of "surface seawater desalination mass production system", as shown in Figures 8 to 10, including: a
實施例4:Embodiment 4:
本實施例給出另外一種〝第一鹽水分離機〞,如圖5、圖6及圖11、圖12所示,該第一鹽水分離機和上述實施例1〝所述深層海水淡化民生用水大量生產系統〞的〝所述第一鹽水分離機5A〞的設備相同,可單獨作為表層海水淡化小量生產使用。
This embodiment provides another "first salt water separator", as shown in Figures 5, 6, 11 and 12. The first salt water separator is the same as the "first
實施例5:Embodiment 5:
本實施例給出另外一種〝第二鹽水分離機〞,如圖6、圖7所示,該第二鹽水分離機和上述實施例1〝所述深層海水淡化民生用水大量生產系統〞的〝所述第二鹽水分離機5B〞的設備相同,可單獨作為表層海水淡化小量生產使用。
This embodiment provides another "second salt water separator", as shown in Figures 6 and 7. The second salt water separator is the same as the "second
以上內容是結合具體的優選實施方式對本發明所作的進一步詳 細說明,不能認定本發明的具體實施只局限於這些說明。對於本發明所屬技術領域的普通技術人員來說,在不脫離本發明構思的前提下,還可以做出若干簡單推演或替換,都應當視為屬於本發明的保護範圍。 The above content is a further detailed description of the present invention in combination with specific preferred implementation methods. It cannot be determined that the specific implementation of the present invention is limited to these descriptions. For ordinary technical personnel in the technical field to which the present invention belongs, they can make some simple deductions or substitutions without departing from the concept of the present invention, which should be regarded as belonging to the protection scope of the present invention.
1:發電系統 1: Power generation system
2:虹吸管機構 2: Siphon mechanism
21:固定座 21: Fixed seat
3:海水儲存池 3: Seawater storage tank
31:輸水管 31: Water pipes
4:高壓重力沉澱池 4: High-pressure gravity sedimentation tank
4A:第一高壓重力沉澱池 4A: The first high-pressure gravity sedimentation tank
4B:第二高壓重力沉澱池 4B: Second high-pressure gravity sedimentation tank
A1:第一下池 A1: First time in the pool
B1:第二下池 B1: Second pool
A2:第一上池 A2: First upper pool
B2:第二上池 B2: Second upper pool
41:輸水管 41: Water pipe
42:海水排水管 42: Seawater drainage pipe
46:半透膜隔離板 46: Semipermeable membrane separator
47:排水電動閘門 47: Drainage electric gate
5A:第一鹽水分離機 5A: First salt water separator
51:淡水輸水管 51: Fresh water pipeline
52:鹵水輸水管 52:Brine pipe
53:噴霧龍頭 53: Spray faucet
58:冷凍壓縮機 58: Freeze compressor
6:淡水儲存池 6: Fresh water storage tank
61:淡水第一輸出管 61: Fresh water first output pipe
62:淡水第二輸出管 62: Fresh water second output pipe
63:半透膜清洗管 63: Semipermeable membrane cleaning tube
7:鹵水儲存池 7:Brine storage tank
71:鹵水輸出管 71:Brine output pipe
Claims (9)
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| TW111126894A TWI842017B (en) | 2022-07-18 | 2022-07-18 | Mass production system of deep sea water desalination for people's livelihood |
| PCT/IB2023/056346 WO2024018302A1 (en) | 2022-07-18 | 2023-07-10 | Mass production system of deep-sea water desalination for domestic water use |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| TW111126894A TWI842017B (en) | 2022-07-18 | 2022-07-18 | Mass production system of deep sea water desalination for people's livelihood |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| TW202404909A TW202404909A (en) | 2024-02-01 |
| TWI842017B true TWI842017B (en) | 2024-05-11 |
Family
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| TW111126894A TWI842017B (en) | 2022-07-18 | 2022-07-18 | Mass production system of deep sea water desalination for people's livelihood |
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| TW (1) | TWI842017B (en) |
| WO (1) | WO2024018302A1 (en) |
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| CN119018965B (en) * | 2024-10-23 | 2024-12-20 | 淮北矿业绿色化工新材料研究院有限公司 | A system and method for concentrating and treating wastewater from an evaporation pond |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20140339169A1 (en) * | 2013-05-15 | 2014-11-20 | Fevzi Zeren | Large volume sub-sea water desalination reverse osmosis system, methods, and apparatus |
| CN104649447A (en) * | 2014-11-25 | 2015-05-27 | 程金生 | Treatment system for sea water desalination and water purification |
| TWM642200U (en) * | 2022-07-18 | 2023-06-11 | 王子信 | Mass production system of deep ocean water desalination for people's livelihood |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104176847A (en) * | 2013-05-21 | 2014-12-03 | 宁波江东索雷斯电子科技有限公司 | Seawater desalination technology |
| CN204211514U (en) * | 2014-10-30 | 2015-03-18 | 珠江水利委员会珠江水利科学研究院 | A kind of sea water desalinating plant |
| CN205045857U (en) * | 2015-10-18 | 2016-02-24 | 李效雨 | Depth of water pressure reverse osmosis seawater desalts system |
| CN111732213A (en) * | 2020-06-10 | 2020-10-02 | 烟台中集来福士海洋工程有限公司 | Seawater Desalination Platform |
-
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- 2022-07-18 TW TW111126894A patent/TWI842017B/en active
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Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20140339169A1 (en) * | 2013-05-15 | 2014-11-20 | Fevzi Zeren | Large volume sub-sea water desalination reverse osmosis system, methods, and apparatus |
| CN104649447A (en) * | 2014-11-25 | 2015-05-27 | 程金生 | Treatment system for sea water desalination and water purification |
| TWM642200U (en) * | 2022-07-18 | 2023-06-11 | 王子信 | Mass production system of deep ocean water desalination for people's livelihood |
Non-Patent Citations (1)
| Title |
|---|
| 譯著 Ahmad, Mansour M. M. Assessment of Freezing Desalination Technologies. Swansea University. 2012. * |
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| WO2024018302A1 (en) | 2024-01-25 |
| TW202404909A (en) | 2024-02-01 |
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