TW478948B - Hybrid distillation method and apparatus - Google Patents
Hybrid distillation method and apparatus Download PDFInfo
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- TW478948B TW478948B TW89127107A TW89127107A TW478948B TW 478948 B TW478948 B TW 478948B TW 89127107 A TW89127107 A TW 89127107A TW 89127107 A TW89127107 A TW 89127107A TW 478948 B TW478948 B TW 478948B
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/14—Treatment of water, waste water, or sewage by heating by distillation or evaporation using solar energy
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/26—Multiple-effect evaporating
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/10—Vacuum distillation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/42—Regulation; Control
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0033—Other features
- B01D5/0036—Multiple-effect condensation; Fractional condensation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D5/00—Condensation of vapours; Recovering volatile solvents by condensation
- B01D5/0033—Other features
- B01D5/0051—Regulation processes; Control systems, e.g. valves
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/16—Treatment of water, waste water, or sewage by heating by distillation or evaporation using waste heat from other processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/02—Foam dispersion or prevention
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/20—Controlling water pollution; Waste water treatment
- Y02A20/208—Off-grid powered water treatment
- Y02A20/212—Solar-powered wastewater sewage treatment, e.g. spray evaporation
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
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- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
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Abstract
Description
478948 A7 __B7__ 五,‘、發明說明(丨) 本發明係有關於一綜合蒸镏方法及裝置。 本發明係特別適用於,但不限於,用以提供純水、食 物或其他物質的冷藏及/或冰凍、空調及/或熱水的一方 法與裝置。 5 由於世界人口的急遽增加,大城市供水管線之老化與 損壞,以及由現代工業與農業所造成之環境污染,許多已 開發及開發中國家正面臨新鮮及潔淨飲用水短缺的危機。 面臨工業廢料不斷增加,以及清潔飲用水之需求的不斷增 加,許多公共供水設備並沒有資源來去除自來水(或可飲 10 用水)中之細菌、病毒、寄生蟲、重金屬、聚合物單體、 輻射物質等。 1998年八月在澳洲雪梨市、以最大且最先進之過濾設 備處理的自來水中被發現含有鞭毛蟲與隱蔽孢子蟲,此自 來水在可供安全飲用之前必須加以煮沸一分鐘以上,這事 15 件影響超過三百萬人。 另一次水污染疾病的爆發是發生在1993年美國威斯 康辛州的密爾瓦基市,它是由於飲用受污染的自來水所造 成,這事件造成超過100人死亡,並且影響半個城市的人 口(大約有430, 000人)。 20 吾人相信這些事件將會在世界上的每一個城市中發 生,經由水散布的毒物與疾病將會繼續在未來對人造成許 多健康上的問題,因此淨化受污染的水及供應大眾高品質 的飲用水是很重要的,目前這是世界性的話題且必須立即 解決的。 第4頁 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) I I I -11ΙΛ----^----I---I (請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 478948 A7 B7 _ 五、發明說明(i) 淨水設備必須符合幾項要求,該設備必須耐用且是自 動化的,該設備也應是多用途的且可以處理不同種類的工 業廢水。該設備應.·能便宜地製造並且可以高效率地提供高 純度的水,來自該設備之廢料應可妾全地排放或可以一經 5 濟的方式進一步處理,該設備本身應易於維護與清潔。 逆滲透水過濾系統是普遍運用於目前的並且可輕易取 得的,它使用過濾器及滲透膜以藉由過濾移除受污染之水 中的雜質,逆滲透水過濾系統需要保持一廢水對產出水的 高比例,通常是3比1,這表示該系統釋出來源水的75°/〇 ίο 以回收25%的純水。此外,使用過的滲透膜無法再循環使 用並且成為一環境污染物。 傳統的蒸餾設備在大氣壓下於l〇〇°C煮沸生水,該設 備消耗相當多的能量來煮沸水,並且也需要大量的冷卻水 來冷凝水蒸氣,該冷卻水在以往是被運送到一儲存水池或 15 槽中,在該儲存水池或槽中,因為使用過的冷卻水的高 溫,可能會滋生藻類。此外,傳統的100°c蒸餾方法無法 被用來處理可燃性溶劑--這是因為高燃性的溶劑會導致爆 炸。 曾有人提出在真空中接近室溫的溫度下蒸餾生水,但 20 是,這種設計需要大量的水來冷凝水蒸氣並且在回收冷卻 水時消耗大量能量。 本發明所提出之設備是設計用來提供以下一或多件 事:便宜、高品質的蒸顧飲用水;熱水,例如,供淋浴之 熱水;家庭中食物之冷藏及/或冰凍;及/或建築物之空 第5頁 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -------------裝----Λ----訂---------線 (請先閱讀背面之注意事項再填寫本頁) 478948 A7 '’_B7_ 五、發明說明($ ) 調。 本發明一較佳目的是這綜合設備之運轉成本係比現有 個別裝置之運轉成本低得多。, 本發明另一較佳目的是該綜合設備係適用於家庭、學 5 校、社區、離島、工廠、船舶及醫院。 • 本發明再一較佳目的是該綜合設備也可用於處理工業 . 廢水,回收·及再生溶劑及/或濃縮污水或工業有毒廢水, 其中該被回收的蒸餾水可以再生,並且剩餘的廢物可以經 濟地移除或儲存。 10 本發明再另一目的是該綜合設備也可以用來淡化海水 使其可以飲用,其中,如由100公升之海水可以多次蒸鶴 ^ 得到的75公升的水,剩餘的,如25公升的濃縮海水可以 接著被用來萃取具有經濟價值的鹽。 ^ 其他的較佳目的將可由以下說明來了解。 15 在一方面,本發明係一種綜合蒸餾方法,其中: 具有至少一壓縮機的一冷藏裝置,將冷媒泵經在一蒸 餾裝置之一煮沸室中的至少一加熱管,該煮沸室係藉由真 空抽取裝置保持在低於大氣壓之壓力下以使得生水在接近 室溫下蒸餾; ί 20 該生水被轉變成一蒸氣,該蒸氣被傳送到該蒸餾裝置 :之一冷凝室中;以及 [該蒸氣藉由在該冷凝室中之冷凝管被冷凝成一液體蒸 ί 餾水,該冷媒係被泵經在一冷凝器下游之冷媒冷凝管,並 i 且回到該壓縮機。 1 第6頁 本紙張尺度適用中.國國家標準(CNS)A4規格(210 X 297公釐) I I------I IVT I I ^ ---I I I I I I (請先閱讀背面之注意事項再填寫本頁) 478948 A7 _B7^_ 五、發明說明() (請先閱讀背面之注意事項再填寫本頁) 較佳地,欲被蒸餾之該生水的一部份係由一供應源經 由在該冷凝室中之生水冷凝管被抽到該冷凝室中,以便在 被送到該煮沸室之,前協助冷凝該蒸氣。 較佳地,通過該生水冷凝管之生水將該冷凝室之一部 5 份熱傳送到該煮沸室以減少用以加熱該生水來蒸餾所需要 的能量輸入。 較佳地,該生水之一部份係藉一生水泵循環流經一真 空抽取裝置及一生水槽,該真空抽取裝置係連接到該煮沸 室以降低在該煮沸室中之壓力。 10 較佳地,該蒸餾水之一部份係藉一蒸餾水泵循環流經 一真空抽取裝置及一蒸餾水槽,該蒸餾水泵係可操作地連 接到該煮沸室以降低在該冷凝室中之壓力。 較佳地,泡沫感應裝置係設置在該冷凝室中以偵測在 進入該冷凝室之蒸氣中的任何污染物,並且係可操作地連 15 接污染排除裝置以便將所有受污染之蒸餾水引流到該生水 槽中。 較佳地,來自該冷凝器之冷媒的一部份由在該冷凝室 中之冷媒冷凝管引流出來以冷卻該生水槽及/或該蒸餾水 槽。 經濟部智慧財產局員工消費合作社印製 20 較佳地,冷媒流經加熱管後用以加熱在一熱水儲存槽 中之水,以第一電磁閥裝置控制該冷凍裝置之冷凝器直到 在該熱水儲存槽中之水到達一預設溫度為止。 較佳地,在該熱水儲存槽中之水也可藉由一風力推動 之泵,而流經至少一太陽能板之流體所加熱。; 第7頁 本紙張尺度適用申國國家標準(CNS)A4規格(210 X 297公釐) 478948 A7 ♦ -_B7_ 五、發明說明(f ) 較佳地,在通過該冷凝器之後,該冷媒可選擇性地通 過一冷藏/冰凍單元及/或一空調單元。 在另一方面,本發明是一綜合蒸餾裝置,其包括: 一蒸鶴裝置,其具有供欲被蒸顧之生水用的一煮沸室 5 及用以收集來自該生水之蒸餾水的一冷凝室; 」 ‘一真空裝置,其係與該蒸餾裝置連接以減少在該蒸餾 裝置中之壓力,以使該生水在大致室溫下進行蒸餾;以及 一冷藏裝置,其具有至少一壓縮機以將冷媒泵經在該 煮沸室中之至少一加熱管、一冷凝器、及在該冷凝室中之 10 至少一冷凝管;此配置使得: 在該蒸餾裝置中之低壓下,被泵經該加熱管的冷媒使 在該煮沸室中之生水沸騰以產生被在該冷凝室中之冷凝管 ^ 冷凝成液體蒸餾水的蒸氣。 - 較佳地,該蒸餾裝置還包括: 15 在該冷凝室中之多數生水冷凝管,使得該生水之一部 份通過該等生水冷凝管以便在該被部份加熱之生水被送到 欲蒸餾之煮沸室之前,幫助該蒸氣冷凝成該液體蒸餾水。 較佳地,該真空裝置包括: 一真空抽取裝置,其係可操作地連接·到該煮沸室以減 ί 20 少在其中的壓力,生水係藉一生水泵流經該生水槽。 [ 較佳地,該真空裝置還包括: I 一真空抽取裝置,其係可操作地連接該冷凝室以減少 ; 在其中的壓力,蒸餾水係藉一蒸餾水槽流經該真空抽取裝 ί 置及一蒸餾水槽。 , r 卜478948 A7 __B7__ V. ‘Invention description (丨) The present invention relates to a comprehensive steaming method and device. The present invention is particularly applicable to, but not limited to, a method and apparatus for providing refrigeration and / or freezing, air conditioning, and / or hot water for pure water, food, or other substances. 5 Due to the rapid increase in the world population, the aging and damage of water supply pipelines in large cities, and the environmental pollution caused by modern industry and agriculture, many developed and developing countries are facing a crisis of shortage of fresh and clean drinking water. Faced with increasing industrial waste and increasing demand for clean drinking water, many public water supply equipment do not have the resources to remove bacteria, viruses, parasites, heavy metals, polymer monomers, radiation from tap water (or drinkable water) Substance, etc. In August 1998, flagellans and cryptic spores were found in tap water treated with the largest and most advanced filtering equipment in Sydney, Australia. This tap water must be boiled for more than one minute before it is safe to drink. 15 cases Affects more than three million people. Another water pollution outbreak occurred in Milwaukee, Wisconsin, USA in 1993. It was caused by drinking contaminated tap water. This incident killed more than 100 people and affected half of the city ’s population (about (430,000 people). 20 I believe that these events will occur in every city in the world. The poisons and diseases spread through water will continue to cause many health problems for people in the future. Therefore, we will purify polluted water and supply high-quality public Drinking water is important, and currently it is a worldwide topic and must be addressed immediately. Page 4 This paper size is in accordance with Chinese National Standard (CNS) A4 (210 X 297 mm) III -11 IΛ ---- ^ ---- I --- I (Please read the precautions on the back before filling in this Page) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 478948 A7 B7 _ V. Description of the Invention (i) Water purification equipment must meet several requirements. The equipment must be durable and automated. The equipment should also be multipurpose and Can treat different kinds of industrial wastewater. The equipment should be able to be manufactured inexpensively and can provide high-purity water with high efficiency. Waste from the equipment should be fully discharged or can be further processed economically. The equipment itself should be easy to maintain and clean. Reverse osmosis water filtration systems are commonly used today and are easily available. It uses filters and osmosis membranes to remove impurities from contaminated water by filtration. Reverse osmosis water filtration systems need to maintain a wastewater to produce water A high ratio, usually 3 to 1, means that the system releases 75 ° / 〇ίο of the source water to recover 25% pure water. In addition, the used permeable membrane cannot be recycled and becomes an environmental pollutant. Traditional distillation equipment boils raw water at 100 ° C at atmospheric pressure. This equipment consumes considerable energy to boil water, and also requires a large amount of cooling water to condense water vapor. This cooling water was previously transported to a In storage tanks or tanks, algae may grow in this storage tank or tank due to the high temperature of the used cooling water. In addition, traditional 100 ° C distillation methods cannot be used to handle flammable solvents-this is because highly flammable solvents can cause explosions. It has been proposed to distill raw water at a temperature close to room temperature in a vacuum, but this design requires a large amount of water to condense water vapor and consumes a lot of energy when recovering cooling water. The device proposed by the present invention is designed to provide one or more of the following: cheap, high-quality steamed drinking water; hot water, such as hot water for showers; refrigeration and / or freezing of food in households; and / Or the empty space of the building page 5 This paper size is applicable to China National Standard (CNS) A4 (210 X 297 mm) ------------- installation ---- Λ --- -Order --------- line (please read the notes on the back before filling this page) 478948 A7 '' _B7_ V. Description of Invention ($) Tune. A preferred object of the present invention is that the operating cost of this integrated equipment is much lower than the operating cost of existing individual devices. Another preferred object of the present invention is that the integrated equipment is suitable for homes, schools, communities, outlying islands, factories, ships and hospitals. • A further preferred object of the present invention is that the integrated equipment can also be used to treat industry. Wastewater, recovery and regeneration solvents and / or concentrated wastewater or industrial toxic wastewater, where the recovered distilled water can be regenerated and the remaining waste can be economically Remove or store. 10 Yet another object of the present invention is that the integrated equipment can also be used to desalinate seawater and make it drinkable. Among them, for example, 75 liters of water obtained by steaming a crane from 100 liters of seawater multiple times, and the remaining, such as 25 liters of water Concentrated seawater can then be used to extract economically valuable salts. ^ Other preferred purposes will be understood from the description below. 15 In one aspect, the present invention is an integrated distillation method, in which: a refrigerating device having at least one compressor is pumped with a refrigerant through at least one heating pipe in a boiling chamber of a distillation device, the boiling chamber is The vacuum extraction device is maintained at a pressure below atmospheric pressure so that the raw water is distilled near room temperature; 20 the raw water is converted into a vapor, which is sent to the distillation device: a condensation chamber; and [The The vapor is condensed into a liquid distilled water by a condenser tube in the condensation chamber. The refrigerant is pumped through a refrigerant condenser tube downstream of a condenser, and returns to the compressor. 1 Page 6 The paper size is applicable. National National Standard (CNS) A4 (210 X 297 mm) I I ------ I IVT II ^ --- IIIIII (Please read the precautions on the back before (Fill this page) 478948 A7 _B7 ^ _ V. Description of the invention () (Please read the notes on the back before filling this page) Preferably, a part of the raw water to be distilled is supplied by a source through The raw water condensing pipe in the condensing chamber is pumped into the condensing chamber to assist in condensing the vapor before being sent to the boiling chamber. Preferably, 5 parts of heat from one part of the condensing chamber through raw water passing through the raw water condensation pipe is transferred to the boiling chamber to reduce the energy input required to heat the raw water for distillation. Preferably, a part of the raw water is circulated by a raw water pump through a vacuum extraction device and a raw water tank, and the vacuum extraction device is connected to the boiling chamber to reduce the pressure in the boiling chamber. 10 Preferably, a part of the distilled water is circulated through a vacuum extraction device and a distilled water tank by a distilled water pump, and the distilled water pump is operatively connected to the boiling chamber to reduce the pressure in the condensing chamber. Preferably, the foam sensing device is arranged in the condensing chamber to detect any contaminants in the vapor entering the condensing chamber, and is operatively connected to a contamination exclusion device to drain all contaminated distilled water to The raw sink. Preferably, a part of the refrigerant from the condenser is drained by a refrigerant condenser tube in the condensation chamber to cool the raw water tank and / or the distilled water tank. Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs. 20 Preferably, the refrigerant flows through the heating pipe to heat the water in a hot water storage tank. The first solenoid valve device controls the condenser of the freezing device until the The water in the hot water storage tank reaches a preset temperature. Preferably, the water in the hot water storage tank can also be heated by the fluid flowing through at least one solar panel by a wind-driven pump. ; Page 7 This paper size applies to the national standard of China (CNS) A4 (210 X 297 mm) 478948 A7 ♦ -_B7_ V. Description of the invention (f) Preferably, the refrigerant can pass through the condenser Optionally through a refrigeration / freezing unit and / or an air conditioning unit. In another aspect, the present invention is a comprehensive distillation device comprising: a steaming crane device having a boiling chamber 5 for raw water to be steamed and a condensation chamber for collecting distilled water from the raw water; "A vacuum device is connected to the distillation device to reduce the pressure in the distillation device, so that the raw water is distilled at approximately room temperature; and a refrigerating device having at least a compressor to cool the refrigerant The pump passes through at least one heating pipe in the boiling chamber, a condenser, and 10 at least one condenser pipe in the condensation chamber; this configuration allows: at a low pressure in the distillation unit, the pump to be pumped through the heating pipe The refrigerant boils the raw water in the boiling chamber to generate a vapor that is condensed into a liquid distilled water by a condensation pipe ^ in the condensation chamber. -Preferably, the distillation device further comprises: 15 a plurality of raw water condensation pipes in the condensation chamber, so that a part of the raw water passes through the raw water condensation pipes so that the raw water heated in the partially heated water is Before being sent to the boiling chamber to be distilled, the steam is condensed into the liquid distilled water. Preferably, the vacuum device includes: a vacuum extraction device operatively connected to the boiling chamber to reduce the pressure therein, and the raw water flows through the raw water tank by a raw water pump. [Preferably, the vacuum device further includes: I a vacuum extraction device operatively connected to the condensation chamber to reduce; the pressure therein, the distilled water flows through the vacuum extraction device through a distilled water tank and a Distilled water tank. , R BU
L \ 第8頁 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) I-----4--^---------線 (請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 478948 A7 B7___ 五、發明說明(fc) 較佳地,該冷藏裝置具有一第一電磁閥裝置,其可操 作以選擇性地引導已通過該冷凝器之冷媒到該冷凝管及/ 或到分別在該生水,槽及蒸餾水槽的冷凝管,以冷卻在該生 水槽及蒸鶴水槽中之生水及蒸餾水。 5 較佳地,該蒸餾裝置包括: 在該煮沸室及該冷凝室之間的多數防泡沫及/或污染 感應器;以及 污染排除裝置,其可由該等感應器來控制以便將所有 受污染之液體蒸餾水引流到該生水槽中,以防止在該蒸餾 10 水槽中之蒸德水的污染。 較佳地,該蒸餾裝置還包括: 一熱水儲存槽,其具有在熱水中的至少一加熱管; 一水之本體,該加熱管係設置在該煮沸室中之加熱管 及該冷凝器之間;以及 15 第二電磁閥裝置,係其可操作以隔離該冷凝器而將冷 媒引導到該熱水加熱管以加熱該水本體。 較佳地,該蒸餾裝置還包括: 一冷藏/冰凍單元;以及 第三電磁閥裝置,其係可操作以引導已通過該冷凝器 20 之冷媒到該冷藏/冰凍單元。 較佳地,該蒸顧裝置還包括: 一空調單元;以及 第四電磁閥裝置,其係可操作以引導已通過該冷凝器 之冷媒到該空調單元。 f 第9頁 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) ί 1 ^ -----/------------^ (請先閱讀背面之注意事項再填寫本頁) 478948 A7 B7 五、發明說明( 較佳地,該蒸餾裝置還包括: 一太陽能加熱板及一可藉風力推動之泵送裝置以使熱 水流經該熱水儲存槽以幫助加熱該水本體可藉風力推動 之。 5 較佳地,該泵送裝置係被一風及/或對流-動力風扇 所驅動。 較佳地,該蒸餾裝置包括: 在該煮沸室中之水位感應裝置,其係可操作地連接煮 沸室的一入口閥;以及 10 控制裝置,與該感應裝置連接,以便在該煮沸室中之 液位超過一預設值時關閉該入口閥。 在整個說明書中,該用語”冷藏裝置”應包括π熱泵π。 為了能完全了解本發明,以下將配合附圖說明多個較 佳實施例,其中: 15 第1圖是本發明第一實施例的流程圖; 第2(a)圖是使用在該第一實施例中之一機械浮球開關 的一示意圖; 第2(b)圖是類似於一電容水位開關的一類似圖; 第3圖是一風驅動泵之一示意圖; 20 第4圖是本發明第二實施例的流程圖; 第5圖是本發明第三實施例的流程圖;以及 第6圖是本發明第四實施例的流程圖。 本發明第一較佳實施例系統之流程圖係顯示在第1圖 中,該厚黑線代表冷媒線,該(熱泵)系統使用泠媒做為媒 ^-----「-----------^ (請先閱讀背面之注意事項再填寫本頁)L \ page 8 This paper size applies to China National Standard (CNS) A4 (210 X 297 mm) I ----- 4-^ --------- line (please read the Please fill in this page again) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 478948 A7 B7___ V. Description of Invention (fc) Preferably, the refrigerating device has a first solenoid valve device which is operable to selectively guide The refrigerant that has passed through the condenser goes to the condensing pipe and / or to the condensing pipes in the raw water tank and the distilled water tank, respectively, to cool the raw water and distilled water in the raw water tank and the steaming crane water tank. 5 Preferably, the distillation device comprises: a majority of anti-foam and / or pollution sensors between the boiling chamber and the condensation chamber; and a pollution exclusion device which can be controlled by the sensors to remove all contaminated Liquid distilled water is drained into the raw water tank to prevent contamination of distilled water in the distilled water tank. Preferably, the distillation device further includes: a hot water storage tank having at least one heating tube in hot water; a body of water, the heating tube being a heating tube and the condenser arranged in the boiling chamber Between; and 15 a second solenoid valve device that is operable to isolate the condenser and direct a refrigerant to the hot water heating tube to heat the water body. Preferably, the distillation device further includes: a refrigerating / freezing unit; and a third solenoid valve device operable to guide the refrigerant that has passed through the condenser 20 to the refrigerating / freezing unit. Preferably, the steaming device further comprises: an air conditioning unit; and a fourth solenoid valve device operable to guide the refrigerant that has passed through the condenser to the air conditioning unit. f page 9 This paper size is applicable to Chinese National Standard (CNS) A4 (210 X 297 mm) ί 1 ^ ----- / ------------ ^ (Please read the back first Note: Please fill in this page again) 478948 A7 B7 V. Invention description (preferably, the distillation device also includes: a solar heating plate and a pumping device that can be driven by wind to make hot water flow through the hot water storage tank To help heat the water body, it can be driven by wind. 5 Preferably, the pumping device is driven by a wind and / or convection-powered fan. Preferably, the distillation device comprises: A water level sensing device that is an inlet valve operatively connected to the boiling chamber; and 10 control devices that are connected to the sensing device to close the inlet valve when the liquid level in the boiling chamber exceeds a preset value. In the description, the term "refrigerator" should include π heat pump π. In order to fully understand the present invention, a number of preferred embodiments will be described below with reference to the drawings, of which: 15 FIG. 1 is a flow chart of the first embodiment of the present invention Figure; Figure 2 (a) is used in the first embodiment A schematic diagram of a mechanical float switch; Figure 2 (b) is a similar diagram similar to a capacitive water level switch; Figure 3 is a schematic diagram of a wind driven pump; 20 Figure 4 is a second embodiment of the present invention Fig. 5 is a flowchart of the third embodiment of the present invention; and Fig. 6 is a flowchart of the fourth embodiment of the present invention. The flowchart of the system of the first preferred embodiment of the present invention is shown in Fig. 1 In this, the thick black line represents the refrigerant line, and the (heat pump) system uses Ling medium as the medium ^ ----- 「---------------- (Please read the precautions on the back before filling (This page)
i JL 第10頁 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 經濟部智慧財產局員工消費合作社印製 478948 A7 __B7 ___ 五、發明說明(¾) 介將熱由一裝置傳送到另一個裝置,該系統可以使用一或 數個壓縮機傳送該冷媒以達高效率。 這综’合設備可,影響數種不同的操作,依據設定值,這 些操作可以被分成:(i) 一低溫蒸顧流程,(i i) 一熱水流 5 程,(i i i) 一冷藏/冰珠機流程,(iv)—空調流程(v)—太 陽能循環流程。所有這些流程可以同時或依據對系統之需 求以不同的組合來操作,這是藉由以模糊(Fuzzy)邏輯電 路控制該系統來達成,這些係以虛線示意地表示。 以下是各流程之說明。 ίο (i)低溫蒸餾流程 該蒸餾室含有一煮沸室(1)及一冷凝室(2),在該煮沸 室(1)内之多數加熱管(3)可以是銅管、不鏽鋼管或塗覆有 π鐵弗龍(Teflon)”的銅管,加熱管(3)之功用是加熱在該煮 沸室(1)中的生水,各冷媒冷凝管(4)及生水冷凝管(5)係 15 設置在該冷凝室(2)中。這兩種管可以是不鏽鋼管或塗覆 有”鐵弗龍π的銅管,該等冷媒冷凝管(4)及生水冷凝管(5) 之功用是冷凝在該冷凝室(2)中的水蒸氣。nTef 1οηπ是一 註冊商標。 在該低溫蒸餾流程之操作前,該蒸餾水槽(6)應裝有 20 蒸餾水或清潔的自來水,在裝滿該蒸餾水槽(6)及該生水 槽(7)之後,主開關可以接著被開啟以進行蒸餾。 一旦該主開關開啟,該模糊邏輯電路(100)將開啟該 電磁閥裝置(8),並且開啟蒸餾水泵(9)及該生水泵(10)。 生水將流經該生水槽(Ό、在該生水泵(10)中之一真 第11頁 本紙張尺度適用中國國家標準(CNS)A4規格(210 $ 297公釐) ^-----「--t---------^ (請先閱讀背面之注意事項再填寫本頁)i JL page 10 This paper size is in accordance with China National Standard (CNS) A4 (210 X 297 mm) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 478948 A7 __B7 ___ 5. Description of the invention (¾) The device is transferred to another device, and the system can use one or several compressors to transfer the refrigerant for high efficiency. This comprehensive equipment can affect several different operations. Depending on the set values, these operations can be divided into: (i) a low-temperature steaming process, (ii) a hot water flow for 5 processes, and (iii) a refrigeration / ice bead. Machine process, (iv)-air conditioning process (v)-solar cycle process. All of these processes can be operated simultaneously or in different combinations depending on the requirements of the system, which is achieved by controlling the system with fuzzy logic circuits, which are indicated schematically by dashed lines. The following is a description of each process. ίο (i) Low temperature distillation process The distillation chamber contains a boiling chamber (1) and a condensation chamber (2). Most of the heating pipes (3) in the boiling chamber (1) can be copper pipes, stainless steel pipes or coated Copper tube with π Teflon ", the function of the heating tube (3) is to heat the raw water in the boiling chamber (1), each refrigerant condensation tube (4) and the raw water condensation tube (5) are 15 is set in the condensing chamber (2). These two kinds of pipes can be stainless steel pipes or copper pipes coated with "Teflon π", the functions of these refrigerant condenser pipes (4) and raw water condenser pipes (5) It is water vapor condensed in the condensation chamber (2). nTef 1οηπ is a registered trademark. Before the operation of the low temperature distillation process, the distilled water tank (6) should be filled with 20 distilled water or clean tap water. After filling the distilled water tank (6) and the raw water tank (7), the main switch can then be turned on to Distill. Once the main switch is turned on, the fuzzy logic circuit (100) will turn on the solenoid valve device (8), and turn on the distilled water pump (9) and the raw water pump (10). The raw water will flow through the raw water tank (Ό, one of the raw water pumps (10)) Page 11 This paper size applies the Chinese National Standard (CNS) A4 specification (210 $ 297 mm) ^ ----- "--T --------- ^ (Please read the notes on the back before filling this page)
,抽取裝置(⑴及生水系⑽之間,由於該真空抽取裝置 ^所產生之壓力差’在該煮沸室⑴中之空氣將流經τ_ 接頭(12)、流量控.制閥(13)、止逆閥(14)、真空抽取裝置 (11) 、生水泵⑽並且進人生水槽⑺,該空氣接著由'該 生水槽(7)出口逸入大氣中,在該煮濟室(1)中之壓力逐漸 降低。 類似地,由於蒸餾水泵(9)之操作,蒸餾水將流經該 蒸餾水槽(6)、安裝在蒸餾水泵(9)之入口中的一真空抽取 裝置(15)、及蒸德水泵(9)之間。因為由該直空抽取梦置 10⑽所產生之壓力差,在該冷凝室⑵中之空氣將流經該 導電度偵測器(16)、3向電磁閥裝置(丨7)、真空抽取裝置 (15)、瘵餾水泵(9),並且進入該蒸餾水槽(丨6)。該空氣 接著經由該蒸餾水槽(6)之出口逸入大氣中,在該冷凝室 (2)中之壓力逐漸降低。 15 一旦在該煮沸室(1)中之壓力掉落到大氣壓力之下, 來自一供應源的生水將經由該電磁抗垢管(18)、濾網 (19)、電磁閥裝置(8)、及該生水冷凝管(5)而流入該煮沸 室(1)。(在該電磁抗垢管(18)中有一磁場以減少在該煮沸 室(1)中之加熱管(3)上的水垢,該濾網(19)防止在該生水 20 中之任何大顆粒流入該煮沸室(1))。 流入該煮沸室(1)之該生水的一部份也流經Τ-接頭 (12) 、流量控制閥(13)、止逆閥(14)、真空抽取裝置 (11)、及生水泵(10),進入生水槽(7)中。在該槽中之多 餘生水將接著排出經過該生水槽(7)出口到一供應源,藉 第12頁 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) I I I 1 I I I · I I (請先閱讀背面之注咅?事項再填寫本頁) •Ί --線· 經濟部智慧財產局員工消費合作社印製 478948 A7 __B7_ 五、發明說明((〇) 由從該煮沸室(1)排出某些生水,在該煮沸室(1)中之生水 之所有溶解之固體(TDS)濃度可以被控制。該流量控制闊 (13)之開、度可以調整以改變被抽出之生水的量-在該生水 中TDS濃度愈高,該流量控制閥(13)的開度愈大。該流量 5 控制閥(13)之開度也控制所產生之蒸餾水與該排出廢水的 比例。 當在該煮沸室(1)中之壓力低,如60kPa時,被抽入 該煮沸室(1)中之生水的量大於被排出之生水的量。在該 煮沸室(1)中之水位開始逐漸地增加,一旦在該煮沸室(1) 10 中之生水位到達在該水位感應器(20)中之一預設值時,該 模糊邏輯電路(100)將關閉該電磁閥裝置(8)。 在這系統中,該水位感應器(20)(見第2圖)係位在該 煮沸室(1)外側,有兩管路連接該煮沸室(1)及冷凝室(2) 與該水位感應器(20)。該水位感應器(20)包括具有一水位 15 測量裝置,如一機械浮球開關(如第2a圖中所示)或一電 容水位開關(如第2b圖中所示)的一水容器,在使用機械 浮動開關的情況中,該浮球(58)將其著該生水水位上下移 動。如果該浮球(58)到達該柄之頂部,該模糊邏輯電路 (100)將關閉該電磁閥裝置(8)並且阻擋該生水流入該煮沸 20 室(1)中。如果使用的是一電容水位開關,在煮沸室(1)中 之該生水水位係藉由使用電容測量裝置(59)測量該電容來 測定,當所測量到的電容到達預設值時,該電磁閥裝置(8) 將被關閉。吾人以實驗發現在該電容測量裝置(59)及該煮 沸室(1)之間的距離必須至少有數公分以防止來自在該煮 第13頁 本^張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) "" ------------------1--訂--------- (請先閱讀背面之注意事項再填寫本頁) 五、發明說明(丨I) 沸室(1)中之生水的干擾。藉由將該水位感應器(2〇)安裝 在該煮沸室(1)之外側,該水位感應器(20)不會受到在該 煮沸室(1)中之生水之浮動的影響,因此,該電磁閥裝置 (8)將不會因為快速的震盪而損壞。此外,藉由改變該水 5位感應相對該煮沸室(1)的高度,在該煮沸室(丨)中 之生水水位可以調整以處理不同種類的生水。 一旦該電磁閥裝置(8)關閉,不論在該煮沸室(1)中之 生水位為何,至少有一段時間它將不會再開啟。或者,在 該生水被抽入該煮沸室(1)中期間的時間與頻率 10 模糊邏輯電路(100)所預設及控制。 ~ 。當在該蒸餾室中之壓力到達,如95kPa時,該模糊邏 輯電路(1〇〇)將打開該壓縮機(21),開啟電磁閥裝置(22)及 電磁閥裝置(23)兩者,並且關閉電磁閥裝置(24)。來自壓 縮機(21)的冷媒流經該煮沸室(!)中部份真空的加熱管 15 (3),並且在該煮沸室(1)中之生水將在接近室溫的溫'度下 沸騰。該生水的一大部份被轉變成水蒸氣,該水蒸氣將上 升,穿過讀防夾帶網(25)(在該等室(1)與(2)之間^,並且 到達該冷凝室(2)中。該防夾帶網(25)防止在該煮沸室中 之渦流中所產生之液體水滴進入該冷凝室(2)中。 ’力 一對泡泳彳貞測器(26)係設置在該防夹帶網(25)上方, 在一 U形容器令且在該煮沸室(1)上方。一 Ac電流係供應 到該泡沐彳貞測器上’如果有任何泡床、氣泡或生水上升並 且流入該U形容器,在該泡珠積測器(26)與該u形容器之 間將會導電,這將致動該模糊邏輯電路(1〇〇).以關閉該電 第14頁 經濟部智慧財產局員工消費合作社印製 478948 A7 B7 _ 五、發明說明(d) 磁閥裝置(8) —段預設的時間,不論在該煮沸室(1)中之生 水水位為何。這阻擋該生水進入該煮沸室(1),並且防止 泡沫、氣,泡或生卞進入該冷凝室(2),它也防止了當該水 位感應器(20)失效時,生水在該煮沸室(1)中溢流的情 5 形。但是,如在果泡沫偵測器(26)與該U形容器間的導電 持續一預設時間之後,該模糊邏輯電路(100)將關閉該電 磁閥裝置(8)並且關閉蒸餾水泵(9)、生水泵(10)、壓縮機 (21)、及電磁閥裝置(23)。該低溫蒸餾流程便以一安全的 步驟結束了。 10 在該U形容器底部中的多數孔可以讓容納在其中的任 何生水回流到該煮沸室,在該偵測器(26)及該容器之間使 用交流電可減少在該生水中的氧化與還原反應。 在通過該泡沫偵測器(26)之後,該水蒸氣將下降到該 冷凝室(2)中,當該水蒸氣接觸到冷媒冷凝管(4)及生水冷 15 凝管(5)時,它冷凝成為蒸餾水並且掉到該冷凝室(2)的底 部。接著蒸餾水被蒸餾水泵(0)抽出經由該導電度偵測器 (16)、3向電磁閥裝置(17)、真空抽取裝置(15),進入該 蒸餾水槽(6)。如果由該冷凝室(2)中抽出之蒸餾水的導電 度高於在該模糊邏輯電路(100)中的一預設值,該3向電 20 磁閥裝置(17)將開啟並且將該受污染的蒸餾水導至止逆閥 (14),以經由真空抽取裝置(11)、生水泵(10)流入該生水 槽⑺。 來自該等加熱管(3)的冷媒流經該冷媒壓力調整器 (27)、熱水儲存槽(28)、電磁閥裝置(22),並且進入該冷 第15頁 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 裝-------J--訂---------線 (請先閱讀背面之注意事項再填寫本頁) 478948 A7 B7 五、發明說明(丨3 凝器(29)。 該冷媒壓力調整器(27)之功用是調整在該煮沸室(1) 之該等加熱管(3)的冷媒壓力,在該冷凝器(29)上之風扇 (30)與(31)係受該模糊邏輯電路(100)控制,它們被用來減 5 少在該冷凝器(29)中之冷媒的溫度。因此,在該系統中之 餘熱可以被釋放到大氣中,這在使該系統可在一高溫環境 中操作是特別重要的。 來自該冷凝器(29)之冷媒流經該集液器(32)、乾燥器 (33)、膨脹裝置(34),並且進入該冷媒冷凝管(4)。當在 10 該等冷媒冷凝管(4)中時,該冷媒膨脹並且吸收熱,接著 該冷媒流入止逆閥(35)、文氏T型管(36),並且最後回到 該壓縮機(21)中。 來自該冷凝器(29)之冷媒的一部份流經該電磁閥裝置 (23),接著這部份的一部份流入膨脹裝置(37)及在生水槽 15 (7)中之冷卻管(39),而另一部份則流入膨脹裝置(38), 及在該蒸餾水槽(6)中之冷卻管(40),這循環流動之目的 是降低在該生水、槽(7)中之生水的溫度以及在該蒸餾水槽 (6)中之蒸餾水的溫度。然後,這兩冷媒流合併並且流經 止逆閥(35)、文氏T型管(36),並且最後回到壓縮機 20 (21)。 受該模糊邏輯電路(100)控制的該電磁闊裝置(41)將 開啟一段非常短的預設時間,當它被開啟時,來自大氣中 之空氣將流經電磁閥裝置(41)、T_接頭(12),並且進入該 煮沸室(1)。在談空氣之衝擊下,堆積在該煮沸室(1)之底 第16頁 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 裝-----Ί--訂---------線 (請先閱讀背面之注意事項再填寫本頁) 478948 A7 B7 五、發明說明(丨 5 ο 11, Between the extraction device (⑴ and the raw water system ⑽, due to the pressure difference generated by the vacuum extraction device ^), the air in the boiling chamber ⑴ will flow through the τ_ connector (12), flow control valve (13), The check valve (14), the vacuum extraction device (11), the raw water pump ⑽ and enter the living water tank 该, the air then escapes into the atmosphere through the outlet of the raw water tank (7), and in the cooking room (1) The pressure gradually decreases. Similarly, due to the operation of the distilled water pump (9), the distilled water will flow through the distilled water tank (6), a vacuum extraction device (15) installed in the inlet of the distilled water pump (9), and the distilled water pump (9). Because of the pressure difference generated by the vertical air extraction dream set 10⑽, the air in the condensation chamber ⑵ will flow through the conductivity detector (16), 3-way solenoid valve device (丨 7 ), Vacuum extraction device (15), retort water pump (9), and enter the distilled water tank (6). The air then escapes into the atmosphere through the outlet of the distilled water tank (6), in the condensation chamber (2) The pressure gradually decreases. 15 Once the pressure in the boiling chamber (1) drops below atmospheric pressure, come Raw water from a supply source will flow into the boiling chamber (1) through the electromagnetic antiscalant pipe (18), strainer (19), solenoid valve device (8), and the raw water condensation pipe (5). There is a magnetic field in the electromagnetic anti-scale pipe (18) to reduce the scale on the heating pipe (3) in the boiling chamber (1), and the filter (19) prevents any large particles in the raw water 20 from flowing into the Boiling chamber (1)). A part of the raw water flowing into the boiling chamber (1) also flows through the T-connector (12), the flow control valve (13), the check valve (14), and the vacuum extraction device ( 11), and the raw water pump (10), enter the raw water tank (7). The excess raw water in the tank will then be discharged through the raw water tank (7) to an outlet, and the paper size applies on page 12. China National Standard (CNS) A4 Specification (210 X 297 mm) III 1 III · II (Please read the note on the back? Matters before filling out this page) • Ί-Line • Printed by the Consumers ’Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 478948 A7 __B7_ V. Description of the invention ((〇) Dissolve some raw water from the boiling chamber (1), all dissolved solids of raw water in the boiling chamber (1) TDS) concentration can be controlled. The opening and degree of the flow control valve (13) can be adjusted to change the amount of raw water being pumped out-the higher the TDS concentration in the raw water, the more open the flow control valve (13) The opening degree of the flow control valve (13) also controls the ratio of the produced distilled water to the discharged wastewater. When the pressure in the boiling chamber (1) is low, such as 60kPa, it is pumped into the boiling chamber ( The amount of raw water in 1) is greater than the amount of raw water being discharged. The water level in the boiling chamber (1) starts to gradually increase. Once the raw water level in the boiling chamber (1) 10 reaches the water level, When one of the preset values is set in the controller (20), the fuzzy logic circuit (100) will close the solenoid valve device (8). In this system, the water level sensor (20) (see Figure 2) is located outside the boiling chamber (1), and there are two pipes connecting the boiling chamber (1) and the condensation chamber (2) to the water level sensor.器 (20). The water level sensor (20) includes a water container with a water level 15 measuring device, such as a mechanical float switch (as shown in Fig. 2a) or a capacitive water level switch (as shown in Fig. 2b). In the case of a mechanical float switch, the float (58) moves it up and down the raw water level. If the float ball (58) reaches the top of the handle, the fuzzy logic circuit (100) will close the solenoid valve device (8) and block the raw water from flowing into the boiling chamber (1). If a capacitive water level switch is used, the raw water level in the boiling chamber (1) is determined by measuring the capacitance using a capacitance measuring device (59). When the measured capacitance reaches a preset value, the The solenoid valve unit (8) will be closed. I have found through experiments that the distance between the capacitance measuring device (59) and the boiling chamber (1) must be at least a few centimeters to prevent from the Chinese National Standard (CNS) A4 specifications applied on this standard on page 13. 210 X 297 mm) " " ------------------ 1--Order --------- (Please read the precautions on the back first (Fill in this page) 5. Description of the invention (丨 I) The interference of raw water in the boiling chamber (1). By installing the water level sensor (20) on the outside of the boiling chamber (1), the water level sensor (20) is not affected by the floating of the raw water in the boiling chamber (1). Therefore, The solenoid valve device (8) will not be damaged by rapid vibration. In addition, by changing the height of the 5-position sensing of the water relative to the boiling chamber (1), the level of the raw water in the boiling chamber (丨) can be adjusted to treat different kinds of raw water. Once the solenoid valve device (8) is closed, regardless of the level of raw water in the boiling chamber (1), it will not open again for at least some time. Alternatively, the time and frequency during which the raw water is pumped into the boiling chamber (1) 10 are preset and controlled by the fuzzy logic circuit (100). ~. When the pressure in the distillation chamber reaches, for example, 95 kPa, the fuzzy logic circuit (100) will open the compressor (21), open both the solenoid valve device (22) and the solenoid valve device (23), and Close the solenoid valve unit (24). The refrigerant from the compressor (21) flows through a partially evacuated heating tube 15 (3) in the boiling chamber (!), And the raw water in the boiling chamber (1) will be at a temperature close to room temperature. boiling. A large part of the raw water is converted into water vapor, which will rise, pass through the anti-entrainment net (25) (between the chambers (1) and (2) ^, and reach the condensation chamber (2). The anti-entrainment net (25) prevents liquid droplets generated in the vortex in the boiling chamber from entering the condensation chamber (2). Above the anti-entrainment net (25), in a U-shaped container and above the boiling chamber (1). An Ac current is supplied to the bubble tester 'if there is any bubble bed, bubbles or The raw water rises and flows into the U-shaped container, and there will be electrical conduction between the bead accumulator (26) and the U-shaped container, which will actuate the fuzzy logic circuit (100). Printed on page 14 printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 478948 A7 B7 _ V. Description of the invention (d) Magnetic valve device (8)-a preset period of time, regardless of the level of raw water in the boiling chamber (1) This prevents the raw water from entering the boiling chamber (1), and prevents foam, gas, bubbles or raw materials from entering the condensation chamber (2). It also prevents the water from being When the sensor (20) fails, raw water overflows in the boiling chamber (1). However, if the conductivity between the fruit foam detector (26) and the U-shaped container continues for a preset time After that, the fuzzy logic circuit (100) will close the solenoid valve device (8) and turn off the distilled water pump (9), the raw water pump (10), the compressor (21), and the solenoid valve device (23). The low temperature distillation process It ends with a safe step. 10 Most of the holes in the bottom of the U-shaped container allow any raw water contained in it to return to the boiling chamber, using AC power between the detector (26) and the container. It can reduce the oxidation and reduction reactions in the raw water. After passing through the foam detector (26), the water vapor will drop into the condensation chamber (2), when the water vapor contacts the refrigerant condensation pipe (4) When the raw water cools the 15 condenser tube (5), it condenses into distilled water and falls to the bottom of the condensing chamber (2). Then the distilled water is pumped out by the distilled water pump (0) and passes through the conductivity detector (16) and 3-way electromagnetic Valve device (17) and vacuum extraction device (15) enter the distilled water tank (6). The conductivity of the distilled water extracted from the condensing chamber (2) is higher than a preset value in the fuzzy logic circuit (100). The 3-way electric 20 magnetic valve device (17) will open and the contaminated Distilled water is guided to the check valve (14) to flow into the raw water tank 真空 through the vacuum extraction device (11) and the raw water pump (10). The refrigerant from the heating pipes (3) flows through the refrigerant pressure regulator (27). , Hot water storage tank (28), solenoid valve device (22), and enter the cold page 15 This paper size applies to China National Standard (CNS) A4 specifications (210 X 297 mm) Packing ------- J--order --------- line (please read the precautions on the back before filling this page) 478948 A7 B7 V. Description of the invention (3 condenser (29). The function of the refrigerant pressure regulator (27) is to adjust the refrigerant pressure of the heating pipes (3) in the boiling chamber (1), and the fans (30) and (31) on the condenser (29) are subject to The fuzzy logic circuit (100) controls and they are used to reduce the temperature of the refrigerant in the condenser (29). Therefore, the residual heat in the system can be released to the atmosphere, which is particularly important in making the system operable in a high temperature environment. The refrigerant from the condenser (29) flows through the header (32), dryer (33), expansion device (34), and enters the refrigerant condenser tube (4). When in 10 such refrigerant condensing pipes (4), the refrigerant expands and absorbs heat, then the refrigerant flows into the check valve (35), the venturi T-tube (36), and finally returns to the compressor (21 )in. Part of the refrigerant from the condenser (29) flows through the solenoid valve device (23), then part of this part flows into the expansion device (37) and the cooling pipe (15) in the raw water tank (15) 39), while the other part flows into the expansion device (38) and the cooling pipe (40) in the distilled water tank (6). The purpose of this circulating flow is to reduce the water in the raw water and tank (7). The temperature of the raw water and the temperature of the distilled water in the distilled water tank (6). These two refrigerant flows then merge and flow through the check valve (35), the venturi T-tube (36), and finally return to the compressor 20 (21). The electromagnetic wide device (41) controlled by the fuzzy logic circuit (100) will be turned on for a very short preset time. When it is turned on, air from the atmosphere will flow through the solenoid valve device (41), T_ Fitting (12) and enters the boiling chamber (1). Under the impact of air, piled up at the bottom of the boiling chamber (1) page 16 This paper size applies the Chinese National Standard (CNS) A4 specification (210 X 297 mm) Packing ----- Ί--Order- -------- Line (Please read the precautions on the back before filling this page) 478948 A7 B7 V. Description of the invention (丨 5 ο 11
5 IX 經濟部智慧財產局員工消費合作社印製 ο 2 部的固體沈積物將會破裂’破裂的碎片接著被抽出流經過 T-接頭(12)、流量控制閥(13)、止逆閥(14)、真空抽取裝 置(11)、生水泵(丨0)並且最後進入生水槽(了),然後它由 該生水槽(7)出口排出。 該低溫蒸餾流程也可以被用來處理工業廢水、下水道 污水、及有毒廢棄物或淡化海水。為了防止在該生水中之 溶解固體結垢在該等加熱警(3)上或者在該煮沸室(1)之内 側,必須要在該生水中添加防垢劑。該溶劑槽(44)含有抗 垢劑,並且被該模糊邏輯電路(1〇〇)所控制的電磁閥裝置 (43)以預設之時間間隔開啟以添加該抗垢劑於該生水中。 依據被處理之生水種類,抗垢劑之化學組成及抗垢劑之添 加量應加以變化,防泡沫劑也可以添加在該溶劑槽(44)中 以防止在該煮沸室(1)中形成泡沫。 一儲存槽可以連接在該蒸餾水槽(6)之出口以儲存蒸 餾水,如果儲存槽滿了,該模糊邏輯電路(1〇〇)將關閉該 電磁閥裝置(8)及電磁閥裝置(23),並且關閉蒸餾水泵 (9)、生水泵(10)、以及壓縮機.(21),然後,結束該低溫 蒸餾流程。 (i i)熱水流程. 有一溫度感應器(28a)安裝在一熱水儲存槽(28)中, 當在該熱水儲存槽(28)中之水的溫度低於一預設溫度時, 該模糊邏輯電路(100)將關閉該電磁閥裝置(22)且開啟該 電磁闊裝置(24),來自該壓縮機(21)之冷媒流經該等加熱 管(3)、冷媒壓力調整器(27),並且進入該熱水儲存槽 ^171 本紙張尽度適用中國國豕標準(CNS)A4規格(210 X 297公釐) -------------裝 i—^—tr----------線 (請先閱讀背面之注意事項再填寫本頁) 478948 A7 __B7_ 五、發明說明(丨f) (28) ,在將熱釋放到在該熱水儲存槽(28)中之水之後,該 冷媒接著流經電磁閥裝置(24)並且回到壓縮機(21)。 一旦在該熱水·儲存槽(2 8)中之水的溫度到達該預設值 時,該模糊邏輯電路(100)將關閉該電磁閥裝置(24)並且 5 開啟電磁閥裝置(22)及電磁閥裝置(23)。 (i i i)冷藏/冰凌·機流程 有一溫度感應器(45a)在一冷藏/冰凍機(45)中,當 在該冷藏/冰凍機(45)中之溫度高於一預設值時,該模糊 邏輯電路(1〇〇)將關閉兩電磁閥裝置(23)與電磁閥裝置 10 (24),開啟兩電磁闊裝置(22)及電磁閥裝置(46)。來自該 熱水儲存槽(28)之冷媒流經電磁閥裝置(22)、冷凝器 (29) 、電磁閥裝置(46)、膨脹裝置(37),並且進入冷藏/ 冰凍機(45),在冷藏/冰凍機(45)内,該冷媒膨脹並且吸 收熱,接著它流經感應計(48)、止逆閥(49)、文氏T型管 15 (36)並且回到壓縮機(21)。 當該低溫蒸餾流程與該冷藏/冰凍機流程同時操作 時,來自冷凝器(29)之冷媒的一部份流入電磁闊裝置 (46)、膨脹裝置(47)並且進入冷藏/冰凍機(45)並且其他 的部份流入集液器(32)、乾燥器(33)、膨脹裝置(34)、冷 20 媒冷凝管(4)、及止逆閥(35)。這兩冷媒流合併在該文氏T 型管(36)處,並且回到該壓縮機(21)。 (iv)空調流程 有一溫度感應器(50a)設置在一空調機(50)中,當由 溫度感應器所測量到的室溫高於一預設值時,該模糊邏輯 第18頁 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 裝-----Ί--訂-------1 *線 (請先閱讀背面之注意事項再填寫本頁) 478948 A7 B7 五、發明說明(丨心) 10 15 經濟部智慧財產局員工消費合作社印製 20 電路(100)將關閉兩電磁閥裝置(23)與電磁閥裝置(24),開 啟兩電磁閥裝置(22)與電磁閥裝置(51)。來自該熱水館^ 槽(28)之’冷媒流經電磁閥裝置(22)、冷凝器(29)、電磁闊 裝置(51)、膨脹裝置(52)並且進入空調機(5〇)中,該冷媒 膨脹並且吸收在該空調機(50)中的熱。它接著流經該感應 計(53)、止逆閥(49)、文氏T型管(36)並且回到該壓縮機 (21)。 當該低溫蒸餾流程與該空調機流程同時運作時,來自 冷凝器(29)之冷媒的一部份流入該電磁閥裝置(51)、膨脹 裝置(52)並且進入空調機(50,而其他的部份將流經集液 器(32)、乾燥器(33)、膨脹裝置(34)、冷媒冷凝管(4)、及 止逆閥(35)。這兩冷媒流合併在該文氏τ型管(36)處,並 且回到該壓縮機(21)。 (v)太陽能循環流裎 該太陽能循環流程只在有太陽的日子才操作,在白天 時’在太陽能板(56)中的水被太陽加熱,安裝在屋頂或室 外的一風扇(54)(見第3圖)係被風轉動,該風扇(54)驅動 一栗(55)以使水流動。在太陽板(56)中被加熱的水被該泵 (55)栗送流動到該熱水儲存槽(28),在此它釋出熱到在該 熱水儲存槽(28)中的水,因此,被太陽能板(56)所吸收的 該太%能可以使被用來加熱在使用水做為介質之該熱水儲 存槽(28)中的水。 在本發明第二實施例中,該系統可以由該生水中回收 高百分比的蒸餾水,對在水源受限且水難以取得處的區 第19頁 本紙張尺Μ财國國準(CNS)A4規格(21(^297公餐) -------------裝-----Γ丨丨t——I-----線 (請先閱讀背面之注意事項再填寫本頁)5 IX Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs. 2 The solid deposits in the 2 department will rupture. ), Vacuum extraction device (11), raw water pump (丨 0) and finally enter the raw water tank (L), and then it is discharged from the outlet of the raw water tank (7). The low temperature distillation process can also be used to treat industrial wastewater, sewage sewage, and toxic waste or desalinated seawater. In order to prevent the dissolved solids in the raw water from scaling on the heating alarms (3) or inside the boiling chamber (1), antiscalants must be added to the raw water. The solvent tank (44) contains an antiscalant, and a solenoid valve device (43) controlled by the fuzzy logic circuit (100) is opened at a predetermined time interval to add the antiscalant to the raw water. Depending on the type of raw water being treated, the chemical composition of the antiscalant and the amount of antiscalant should be changed. Antifoaming agents can also be added to the solvent tank (44) to prevent formation in the boiling chamber (1). foam. A storage tank can be connected to the outlet of the distilled water tank (6) to store distilled water. If the storage tank is full, the fuzzy logic circuit (100) will close the solenoid valve device (8) and the solenoid valve device (23). Then, the distilled water pump (9), the raw water pump (10), and the compressor (21) are turned off, and then the low-temperature distillation process is ended. (ii) Hot water flow. A temperature sensor (28a) is installed in a hot water storage tank (28). When the temperature of the water in the hot water storage tank (28) is lower than a preset temperature, the The fuzzy logic circuit (100) will close the electromagnetic valve device (22) and open the electromagnetic wide device (24), and the refrigerant from the compressor (21) flows through the heating pipes (3), the refrigerant pressure regulator (27) ), And enter the hot water storage tank ^ 171 This paper applies to China National Standard (CNS) A4 specifications (210 X 297 mm) as much as possible ------------- 装 i — ^ — tr ---------- line (please read the precautions on the back before filling this page) 478948 A7 __B7_ V. Description of the invention (丨 f) (28) After releasing the heat to the hot water storage After the water in the tank (28), the refrigerant then flows through the solenoid valve device (24) and returns to the compressor (21). Once the temperature of the water in the hot water storage tank (28) reaches the preset value, the fuzzy logic circuit (100) will close the solenoid valve device (24) and 5 open the solenoid valve device (22) and Solenoid valve device (23). (iii) The refrigerating / freezing machine has a temperature sensor (45a) in a refrigerating / freezing machine (45). When the temperature in the refrigerating / freezing machine (45) is higher than a preset value, the blur The logic circuit (100) will close the two solenoid valve devices (23) and the solenoid valve device 10 (24), and open the two solenoid valve devices (22) and the solenoid valve device (46). The refrigerant from the hot water storage tank (28) flows through the solenoid valve device (22), the condenser (29), the solenoid valve device (46), the expansion device (37), and enters the refrigerating / freezing machine (45). In the refrigerator / freezer (45), the refrigerant expands and absorbs heat, then it flows through the induction meter (48), check valve (49), Venturi T-tube 15 (36) and returns to the compressor (21) . When the low temperature distillation process and the refrigerator / freezer process are operated at the same time, a part of the refrigerant from the condenser (29) flows into the electromagnetic wide device (46), the expansion device (47) and enters the refrigerator / freezer (45). And other parts flow into the liquid collector (32), the dryer (33), the expansion device (34), the refrigerant cooling pipe (4), and the check valve (35). The two refrigerant flows are merged at the Venturi T-tube (36) and returned to the compressor (21). (iv) The air conditioning process has a temperature sensor (50a) set in an air conditioner (50). When the room temperature measured by the temperature sensor is higher than a preset value, the fuzzy logic Applicable to China National Standard (CNS) A4 specification (210 X 297 mm) Packing ----- Ί--Order ------- 1 * Line (Please read the precautions on the back before filling this page) 478948 A7 B7 V. Description of the invention (丨 heart) 10 15 Printed by the Intellectual Property Bureau of the Ministry of Economic Affairs Employee Cooperatives 20 Circuit (100) will close the two solenoid valve devices (23) and solenoid valve devices (24), and open the two solenoid valve devices ( 22) With the solenoid valve device (51). The refrigerant from the tank (28) of the hot water hall flows through the solenoid valve device (22), the condenser (29), the electromagnetic wide device (51), the expansion device (52) and enters the air conditioner (50). The refrigerant expands and absorbs heat in the air conditioner (50). It then flows through the sensor (53), check valve (49), Venturi T-tube (36) and back to the compressor (21). When the low temperature distillation process and the air conditioner process operate at the same time, a part of the refrigerant from the condenser (29) flows into the solenoid valve device (51), the expansion device (52) and enters the air conditioner (50, and other Part of it will flow through the collector (32), dryer (33), expansion device (34), refrigerant condenser (4), and check valve (35). These two refrigerant flows are combined in the Venturi τ type Tube (36) and return to the compressor (21). (V) Solar circulation flow. The solar circulation flow is only operated on days with the sun, and during the day 'the water in the solar panel (56) is The sun is heated. A fan (54) (see Figure 3) installed on the roof or outdoors is rotated by the wind. The fan (54) drives a chestnut (55) to make water flow. It is heated in the solar panel (56). The water is pumped by the pump (55) and flows to the hot water storage tank (28), where it releases the water that has been heated to the hot water storage tank (28), and is therefore held by the solar panel (56). The absorbed too much energy can be used to heat water in the hot water storage tank (28) using water as a medium. In the second embodiment of the present invention In this example, the system can recover a high percentage of distilled water from the raw water. For areas where water sources are limited and water is difficult to obtain, page 19 of this paper rule: China Standard (CNS) A4 (21 (^ 297) Meal) ------------- install ----- Γ 丨 丨 t——I ----- line (please read the precautions on the back before filling this page)
,,如沙漠與離島而言,所需要的水淨化系統應可以由水 源儘可能地回收水。類似地,為了處理工業有毒廢水及環 境污染醫療廢水,·回收大部份的水並且留下高濃度、少量 的廢物以便再處理或儲存是較佳的。這不僅可以回收與再 生水,因此減少工廠與醫院所稍耗的水,而且減少剩餘廢 料的運送與處理成本。 ' .這系統也可以被用來將工業廣料漢縮成小容積及高濃 度,為了處理具有不同程度之溶解固體濃度的生水,該流 量控制閥(13)之開度可以調整以改變由該煮沸室(1)排出 10之廢料,該流量控制閥(13)之開度愈小,在該煮沸室(1) 之生水中的總溶解固體濃度愈高。雖然該生水在低溫及在 真空條件下沸騰,在該生水中之總溶解固體濃度將不可避 免地在該等加熱管(3)上產生水垢以及在該煮沸室(丨)之底 邛上的沈積物。因此,該煮濟室(1)將會需要在一段操作 15 時間之後加以清潔。 i.齊曰:^讨麦QInIL肖賢-昨:il印製 ^ · I I I I . (請先閱讀背面之注意事項再填寫本頁) 為了能輕易地移除在該煮沸室(1)之底部的固體沈積 物及在該等加熱管(3)上的水垢,在第1圖中之蒸餾室被 加以變化。如第4圖中所示,該煮沸室(1)與該冷凝室(2) 被分開,該煮沸室(1)可以藉由使該室沿著在框架(63)上 20 的軋道(62)滑動而輕易地被開啟。多數夾具(从)被用來保 持該煮沸室(1)被鎖住,在該煮沸室(1)之底‘處的軋道引 導構件(61)可以沿著該軋道(62)滑動。當該煮沸室(1)之 底部處有固體沈積物並且需要清潔時,該等夾具(6〇)可以 開啟並且該煮濟室(1)滑向右方,接著可以輕,易地進入該 第20頁 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 經濟部智慧財產局員工消費合作社印製 478948 A7 _B7_ 五、發明說明(1?) 煮沸室(1)之底部及該等加熱管(3)以進行清潔。在該煮沸 室(1)之右方有一握把(64)以助該煮沸室(1)滑動。 在此‘設計中,,,一高百分比之生水可以被蒸發及回收。 在第4圖中之.室可以讓該煮沸室(1)輕易地開啟及關閉, 5 接著,在該加熱管(3)上的水垢及在該煮沸室(1)之底部上 的餘留固體沈積物可以輕易地移除。 在本發明第三實施例中,該系統可以使用一或多個蒸 餾室來蒸餾生水,藉由以串聯之方式連接數個蒸餾室,生 水可以在不同的溫度被蒸發及冷凝以產生更多的蒸餾水, 10 輸入能量可以更有效地利用。 如第5圖中所示,來自該電磁閥裝置(8)的生水依序 流入在蒸餾室(C)中之生水冷凝管(5)、在蒸餾室(B)中之 生水冷凝管(5)、在蒸餾室(A)中之生水冷凝管(5),生水 逐漸地被加熱,因此,在該蒸顧室(A)中之生水冷凝管(5) 15 的溫度最熱,接著是在蒸餾室(B)中之生水冷凝管(5)及在 蒸餾室(C)中之生水冷凝管(5)。接著該生水進入在該蒸餾 室(A)中之煮沸室(1),在蒸餾室(A)中未變成蒸氣之剩餘 生水將流入在該蒸餾室(B)中之煮沸室(1)及在該蒸餾室(C) 中之煮沸室(1)〇 20 類似地,來自該膨脹裝置(34)的冷媒流經在該蒸餾室 (C)中之冷媒冷凝管(4)、在該蒸餾室(B)中之冷媒冷凝管 (4)及在該蒸餾室(A)中之冷媒冷凝管(4),因此,在該蒸 餾室(C)中之冷媒冷凝管(4)的溫度將是最冷的,接著在該 蒸餾室(A)中之冷媒冷凝管(4)的溫度將是最高的。 第21頁 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -------------------j---訂--------I (請先閱讀背面之注意事項再填寫本頁) 痤齊茚皆¾讨¾¾員x.^iB^DftFi=p^ 478948 A7 __B7_ 五、發明說明((1) 來自該壓縮機(21)之冷媒將接著流經在蒸餾室(A)中 的加熱管(3)、在蒸德室(B)中之加熱管(3)、及在蒸餾室 (C)中之加熱管(3),。該冷媒逐漸地放熱,因此,在該蒸餾 室(A)之煮沸室(1)中的生水溫度將是最高的,接著是在該 5 蒸餾室(B)之煮沸室(1)中的生水、及蒸餾室(C)之煮沸室 (1)中的生水。 因此,在該·煮沸室(1)及該等冷媒冷凝管(4)中的生水 以及在每一蒸餾室中之冷凝室(2)中之生水冷凝管(5)之間 有一溫度差,因此,在各蒸餾室中之生水可以在不同的溫 1〇 度被蒸發及冷凝。 這些蒸餾室共用相同的插頭部份以排出低揮發性氣體 及所產生的蒸餾水,由各蒸餾室產生之蒸餾水均流入在蒸 餾室(c)中之冷凝室(2)並且接著流入該導電偵測器(16)、 3向電磁闊裝置(17)、真空抽取裝置(15)、蒸餾水泵(9), 15 並且最後流入蒸餾水槽(6)。該等蒸餾室應保持在不同的 高度以助該生水及蒸餾水的流動。 第6圖顯示本發明第四實施例,其中一三階段多閃蒸 熱泵單元可以使用相同的輸入能量(即,相同尺寸的壓縮 機(21)來產生幾乎三倍於單一單元的蒸餾水。 20 該進料水通過在該蒸餾室(C)中之生水冷凝管(5)並且 吸收熱,該進料水吸收來自在該排空清除系統(71)中之熱 交換器(70)的熱並且接著吸收來自取代在蒸餾水槽(6、7) 中使用之冷卻風扇(74、75)且用來冷卻可得到一良好真空 之泵(9、10)之熱交換器(72)冷藏抽吸管線(73)的熱。 第22頁 本紙張尺度適用中國國家標準(CNS)办4規格(210 X 297公釐) " ^------„---^--------!^. (請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 478948 A7 B7 _ 五、發明說明(么〇) 該等槽(6、7)可以藉由流出某些冷媒而被冷卻,在此 應注意的是在室(A)與(B)中,並沒有冷卻管(4、5)設置在 產生在這些室(即:A與B)中且分別在室(B)與(C)中藉由 蒸氣之分子崩塌而由於該進料水之溫度差造成之蒸氣溫度 5 減少且由於在各室中之散熱所造成之冷卻效應而被低壓抽 送的蒸氣上。 本發明之低溫蒸餾流程,其中生水(即,生水)係在高 真空中但在低溫下煮沸,與習知100%蒸餾方法相較,使甩 較少的能源,但產生更多的蒸餾水。該方法避免在逆滲透 1〇 方法中所需之更換過濾器,因此避免了病毒與細菌阻塞及 滋生的問題,同時也將加熱管結垢的情形減至最少。 藉由使該冷媒循環通過該熱水儲存槽,熱可以由該加 熱器傳送到該冷媒,如,當加熱器超過80-85°C時,以便 對該冷媒提供熱,藉此減少對該等壓縮機的工作負載。 15 該壓縮機之選擇係依據在所需之安裝時該系統的能量 循環要求而定並且這些要求係依據,如: (1) 每日所需之蒸餾水量; (2) 每日所需熱水之量; (3) 欲被冷藏/冷卻之產品之體積/種類及大氣條 20 件; (4) 欲加以空調之空間的體積/結構及大氣條件;以 及 (5) 可用之太陽能量而定。 兩個或多個壓縮機可以串聯/並聯使用並且它們的操 第23頁 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -------------裝-----^---訂---------線 (請先閱讀背面之注意事項再填寫本頁) 478948 A7 B7 五 、發明說明(义|In the case of deserts and outlying islands, the required water purification system should be able to recover as much water as possible from the water source. Similarly, in order to treat industrial toxic waste water and environmentally polluted medical waste water, it is better to recover most of the water and leave a high concentration, small amount of waste for reprocessing or storage. This not only recycles and regenerates water, and therefore reduces water consumption in factories and hospitals, but also reduces the cost of transporting and treating excess waste. This system can also be used to reduce industrial materials to small volumes and high concentrations. In order to process raw water with varying degrees of dissolved solids concentration, the opening of the flow control valve (13) can be adjusted to change from The boiling chamber (1) discharges waste material 10, the smaller the opening degree of the flow control valve (13), the higher the total dissolved solid concentration in the raw water of the boiling chamber (1). Although the raw water boils at low temperature and under vacuum conditions, the total dissolved solids concentration in the raw water will inevitably produce scale on the heating pipes (3) and the bottom of the boiling chamber (丨). Sediment. Therefore, the cooking chamber (1) will need to be cleaned after a period of 15 hours of operation. i. Qi Yue: ^ 谈 麦 QInIL 肖 贤-Yesterday: il print ^ · IIII. (Please read the notes on the back before filling this page) In order to easily remove the bottom of the boiling chamber (1) The solid deposits and scale on the heating pipes (3) are changed in the distillation chamber in Fig. 1. As shown in Figure 4, the boiling chamber (1) is separated from the condensation chamber (2), and the boiling chamber (1) can be moved along the rolling path (62) on the frame (63) by 20 ) Slide and easily open. Most fixtures (slave) are used to keep the boiling chamber (1) locked, and the rolling path guide member (61) at the bottom of the boiling chamber (1) can slide along the rolling path (62). When there is solid deposit at the bottom of the boiling chamber (1) and it needs to be cleaned, the clamps (60) can be opened and the cooking chamber (1) slides to the right, and then it can easily and easily enter the first 20 pages of this paper are in accordance with China National Standard (CNS) A4 (210 X 297 mm). Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs. 478948 A7 _B7_ 5. Description of the invention (1?) These heating pipes (3) are used for cleaning. There is a grip (64) to the right of the boiling chamber (1) to help the boiling chamber (1) slide. In this design, a high percentage of raw water can be evaporated and recovered. The chamber in Figure 4 allows the boiling chamber (1) to be easily opened and closed. 5 Next, the scale on the heating tube (3) and the remaining solids on the bottom of the boiling chamber (1) The deposits can be easily removed. In the third embodiment of the present invention, the system can use one or more distillation chambers to distill raw water. By connecting several distillation chambers in series, the raw water can be evaporated and condensed at different temperatures to produce more water. With more distilled water, 10 input energy can be used more efficiently. As shown in Fig. 5, the raw water from the solenoid valve device (8) flows into the raw water condensing pipe (5) in the distillation chamber (C) and the raw water condensing pipe in the distillation chamber (B) in this order. (5) The raw water condensing pipe (5) in the distillation chamber (A), the raw water is gradually heated, so the temperature of the raw water condensing pipe (5) 15 in the steaming chamber (A) is the most The heat is followed by the raw water condenser (5) in the distillation chamber (B) and the raw water condenser (5) in the distillation chamber (C). Then the raw water enters the boiling chamber (1) in the distillation chamber (A), and the remaining raw water that has not become a vapor in the distillation chamber (A) will flow into the boiling chamber (1) in the distillation chamber (B). And the boiling chamber (1) in the distillation chamber (C) Similarly, the refrigerant from the expansion device (34) flows through the refrigerant condensing pipe (4) in the distillation chamber (C), in the distillation The refrigerant condensing pipe (4) in the chamber (B) and the refrigerant condensing pipe (4) in the distillation chamber (A), therefore, the temperature of the refrigerant condensing pipe (4) in the distillation chamber (C) will be The temperature of the coldest refrigerant condenser (4) in the distillation chamber (A) will be the highest. Page 21 This paper size applies to China National Standard (CNS) A4 (210 X 297 mm) ------------------- j --- Order ---- ---- I (Please read the precautions on the back before filling in this page) Acehindenes are all members x. ^ IB ^ DftFi = p ^ 478948 A7 __B7_ 5. Description of the invention ((1) From this compressor The refrigerant of (21) will then flow through the heating pipe (3) in the distillation chamber (A), the heating pipe (3) in the steaming chamber (B), and the heating pipe (C) in the distillation chamber (C) ( 3). The refrigerant is gradually exothermic, so the temperature of the raw water in the boiling chamber (1) of the distillation chamber (A) will be the highest, followed by the boiling chamber (1) of the 5 distillation chamber (B). ), And the raw water in the boiling chamber (1) of the distillation chamber (C). Therefore, the raw water in the · boiling chamber (1) and the refrigerant condenser tubes (4), and in each There is a temperature difference between the raw water condensation pipes (5) in the condensation chamber (2) in the distillation chamber, so the raw water in each distillation chamber can be evaporated and condensed at different temperatures of 10 degrees. These distillation chambers Share the same plug part to vent low volatile gases and the resulting distillation The distilled water produced by each distillation chamber flows into the condensation chamber (2) in the distillation chamber (c) and then flows into the conductive detector (16), the 3-way electromagnetic wide device (17), and the vacuum extraction device (15). The distilled water pumps (9), 15 and finally flow into the distilled water tank (6). The distillation chambers should be maintained at different heights to facilitate the flow of the raw and distilled water. Figure 6 shows a fourth embodiment of the invention, one of which The three-stage multiple flash heat pump unit can use the same input energy (ie, the compressor (21) of the same size) to produce almost three times the distilled water of a single unit. 20 The feed water passes through one of the distillation chambers (C). Raw water condensate (5) and absorbs heat, the feed water absorbs heat from the heat exchanger (70) in the evacuation system (71) and then absorbs heat from the water in the distilled water tanks (6, 7). The cooling fan (74, 75) used is used to cool the heat of the heat exchanger (72) refrigerating suction line (73) which can obtain a good vacuum pump (9, 10). Page 22 This paper size is applicable to China National Standards (CNS) Office 4 specifications (210 X 297 mm) " ^ ------ „--- ^ --------! ^. (Please read the notes on the back before filling out this page) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 478948 A7 B7 _ V. Description of the invention (Mo) The tanks (6, 7) can be cooled by flowing out some refrigerants. It should be noted here that there are no cooling pipes (4) in the chambers (A) and (B). 5) The steam temperature 5 generated in these chambers (ie: A and B) and in the chambers (B) and (C) respectively due to the collapse of the steam molecules due to the temperature difference of the feed water is reduced And due to the cooling effect caused by the heat dissipation in each room, the steam is pumped by the low pressure. According to the low-temperature distillation process of the present invention, raw water (ie, raw water) is boiled at a low temperature in a high vacuum. Compared with the conventional 100% distillation method, less energy is thrown away, but more distilled water is generated. . This method avoids the need to replace the filter in the reverse osmosis 10 method, thus avoiding the problem of virus and bacteria blocking and breeding, and also minimizing the scaling of the heating tube. By circulating the refrigerant through the hot water storage tank, heat can be transferred from the heater to the refrigerant, for example, when the heater exceeds 80-85 ° C, in order to provide heat to the refrigerant, thereby reducing the Workload of the compressor. 15 The selection of the compressor is based on the energy cycle requirements of the system at the time of installation and these requirements are based on, for example: (1) the amount of distilled water required daily; (2) the daily hot water required The amount; (3) the volume / type of the product to be refrigerated / cooled and 20 pieces of atmospheric conditions; (4) the volume / structure and atmospheric conditions of the space to be air-conditioned; and (5) the amount of solar energy available. Two or more compressors can be used in series / parallel and their operation page 23 This paper size applies to China National Standard (CNS) A4 (210 X 297 mm) ------------ -Install ----- ^ --- order --------- line (please read the notes on the back before filling this page) 478948 A7 B7 V. Description of the invention (meaning |
ο -IX 5 11 ο 2 作可以選擇性地被控制,雖然冷藏/冰凍經常是最優先的 順序,但是該”模糊”邏輯電路可以被程式化以改變對各操 作的優先順序。·· 在該冷凝室中之冷媒冷凝管及生水冷凝管可以上下叠 置或交替疊置’該蒸氣先接觸該等生水冷凝管是較佳的, 因為這些生水冷凝管將是具有比該等冷媒冷凝管更高的溫 度,並且在它進入該煮沸室之前會有較多量的熱將會傳送 到該生水。 週期性地將大氣中的空氣注入該煮沸室可以使在該素 沸室之底部的固體沈積物被分割成多塊,並且接著經由真 空抽取裝置及該生水槽釋出到一收集點。這免除了機械刮 除及/或化學蝕除(使用強酸)來移除在該煮沸室上所產生 之任何固體沈積物的必要。 藉由選擇性地將冷媒引導到在該蒸餾水槽中之冷卻 管,並且到在該生水槽中之冷卻管,可確使各泵及真空抽 取裝置之效率得以保持以維持在該蒸餾裝置中之該等煮沸 及冷凝室中的真空。此外,如果有被污染的蒸餾水進入該 槽中時,在該蒸餾水槽中之細菌及/或病毒生長的可能性 減至最低。 較佳地,該冷凝器具有一定速風扇及一變速風扇一該 定速風扇(3G)僅在該壓縮機操作時操作,且受該,,模糊"邏 輯電路⑽)控制為佳。該變逮風扇⑻被壓力控制器⑽ 所控制,並且仙在該冷媒q度超過一預設值時操作為 佳-如果該冷媒溫度太高,那相系統會排出太多熱且蒸 第24頁ο -IX 5 11 ο 2 operations can be selectively controlled. Although refrigeration / freezing is often the highest priority, the "fuzzy" logic circuit can be programmed to change the priority of operations. ·· The refrigerant condensate tubes and raw water condensate tubes in the condensing chamber can be stacked on top of each other or alternately. 'The steam is better to contact the raw water condensate tubes first, because these raw water condensate tubes will have a ratio The refrigerant condensing tube has a higher temperature, and a larger amount of heat will be transferred to the raw water before it enters the boiling chamber. Periodically injecting air from the atmosphere into the boiling chamber allows the solid sediment at the bottom of the boiling chamber to be divided into pieces and then released to a collection point via a vacuum extraction device and the raw water tank. This eliminates the need for mechanical scraping and / or chemical ablation (using a strong acid) to remove any solid deposits produced on the boiling chamber. By selectively directing the refrigerant to the cooling pipe in the distilled water tank, and to the cooling pipe in the raw water tank, it is possible to ensure that the efficiency of the pumps and vacuum extraction devices is maintained to maintain the efficiency in the distillation device. These boiling and condensing vacuums. In addition, if contaminated distilled water enters the tank, the possibility of bacteria and / or viruses growing in the distilled water tank is minimized. Preferably, the condenser has a fixed-speed fan and a variable-speed fan. The fixed-speed fan (3G) is operated only when the compressor is operating, and is controlled by the "fuzzy logic circuit". The variable fan ⑻ is controlled by the pressure controller 并且, and works well when the refrigerant q degree exceeds a preset value-if the refrigerant temperature is too high, the phase system will emit too much heat and steam. Page 24
本紙張尺度適用中國國家標準(CNS)A4規格(210 X -------------裝-----^ —訂·--------線 C請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 478948 A7 B7_ 五、發明說明(^) 餾水之生產將減少。設置該定速風扇(30)與該變速風扇 (31)也會減少嗓音及由於定期開關所造成之損壞。 在該·蒸餾裝艮中揮發性氣體之產生,特別是在該夾帶 過濾器(25)上方,係藉由將蒸氣由該蒸餾裝置之頂部經由 5 該止逆閥(42)及真空抽取裝置(11)旁之T型管(12)抽出來 避免,移除這些蒸氣可將蒸餾水之污染減至最低。 在此要強調的是由具有裙部(26a)之夾帶井所提供的 保護,該裙部藉由在該熱蒸氣上升管中由在冷卻時蒸氣分 子崩塌之壓力差所產生之氣流引導任何沿著該蒸氣缸上升 1〇 之夾帶水滴,藉此如果該等被夾帶之水滴或泡沫等通過該 夾帶網(25)時,這些水滴或泡沫、氣泡等係被該裙部(26a) 引導上升到位於欲被導電偵測器(26)偵測之該夾帶網(25) 正上方的該井(26b)中。該井具有可使正在液化之氣泡回 到該煮沸室(1)的多數孔,該等偵測器具有可利用一電位 15 計調整的一感應AC電壓,該電位計可調整該電壓以配合 導電性之要求,該等偵測器(26)係與該室絕緣並且係保持 與該不鏽鋼井之底部非常靠近(1. 5mm)以便敏感地且快速 地 <貞測。 一低AC電壓被使用,因此該電壓,藉其交替性,不 20 會以電解作用電解地由該等偵測器及該金屬容器轉移金 .屬,因此該塗層可以進行該等偵測器之感應。 在如上所述地偵測在該主系統中之導電性時,由該感 應器進行之該電子設備之開關截斷該進料水經由該進料水 電磁閥裝置(8)到達該煮沸室(1)直到沒有感應到導電性為 第25頁 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -------------裝--------訂---------線 (請先閱讀背面之注意事項再填寫本頁) 478948 A7 B7 g. P |r I 才This paper size applies to China National Standard (CNS) A4 specifications (210 X ------------- install ----- ^-order · -------- line C, please first Read the notes on the back and fill in this page) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 478948 A7 B7_ V. Description of Invention (^) The production of distilled water will be reduced. Setting the constant speed fan (30) and the variable speed fan (31) will also reduce the noise and damage caused by the regular switch. The generation of volatile gases in the distillation device, especially above the entrained filter (25), is achieved by passing steam from the top of the distillation device through the 5 check valve (42) and vacuum extraction device ( 11) The T-tube (12) next to it is drawn out to avoid, removing these vapors can minimize the contamination of distilled water. What is emphasized here is the protection provided by an entrained well with a skirt (26a) which guides any area along the hot vapor riser by the air flow generated by the pressure difference of the vapor molecules collapsing during cooling. The entrained water droplets rising by 10 with the steam cylinder, so that if the entrained water droplets or foams pass through the entrained mesh (25), the water droplets, foams, bubbles, etc. are guided by the skirt (26a) to rise to Located in the well (26b) directly above the entrained net (25) to be detected by the conductive detector (26). The well has a number of holes that allow liquefied bubbles to return to the boiling chamber (1). The detectors have an induced AC voltage that can be adjusted using a potentiometer, which can adjust the voltage to match conductivity. As required by nature, the detectors (26) are insulated from the chamber and are kept very close to the bottom of the stainless steel well (1.5mm) in order to sensitively and quickly < test. A low AC voltage is used, so the voltage, by virtue of its alternation, will not be used to electrolyze gold from the detectors and the metal container by electrolysis, so the coating can perform the detectors. Of induction. When the electrical conductivity in the main system is detected as described above, the switch of the electronic device by the sensor intercepts the feed water to the boiling chamber (1) via the feed water solenoid valve device (8) ) Until the conductivity is not sensed on page 25, the paper size applies the Chinese National Standard (CNS) A4 specification (210 X 297 mm) ------------- install ------ --Order --------- line (please read the precautions on the back before filling this page) 478948 A7 B7 g. P | r I
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五、發明說明 止。但是,如果在時間到之後於開啟時感應到導電性。該 電磁閥(8)將仍維持關閉並且其取消各次及每一次這種感 應的再啟動被偵測,,大約15到20秒直到沸騰穩定且沒有偵 測到夾帶物(泡沫)為止。在各次偵測到導電性時,電磁閥 裝置開啟之取消時間也確使該電磁閥裝置(8)不會在污染 谓測間振盈,藉此防止該閥的不當磨耗。 如果發生溢流,或者在劇烈沸騰時,對污染問題所提 供的另一保護是具有類似於主要者之偵測器的第二導電感 應系統,其指示該等電子設備以便在有超過2到5百萬分 之一之任何被污染蒸餾水通過該冷凝室時引流該被污染的 蒸館水。 蒸餾水將只在該污染值係,例如,低於2ppm時,被 引導回該蒸顧水槽(6),這會發生在偵測到在蒸儲水之 後’如秒。當該方法不是依靠測量在該儲存槽中的導 電性’它比那方法更可靠。 任何被污染之蒸餾水經由位在該蒸餾抽吸管線中且在 該冷凝室(2)及該真空抽取裝置(15)之出口,蒸餾水泵(9) 及該蒸餾水槽(6)之間的該3向引流電磁閥裝置(π)而被 再導流到該生水泵(10)送系統及其生水槽(7)。 土如果該污染被該偵測系統偵測到的話,蒸餾水將被引 流遠離由真空抽取裝置(15)、蒸餾水泵(9)及蒸餾水槽(6) 構成之蒸餾水抽吸泵送系統,因此該蒸餾水槽(6)不合 生污染。 g發 另一個要考慮的流程是在排出出口處防止成晶的I 5 10 15 20 第26頁 本紐尺度適用中國國家標準規格⑵◦ X挪公爱 ^-----------------^ (請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 478948 A7 B7_ 五、發明說明(ΐψ) 置,藉此大氣經由一計時開關之電磁閥裝置(41)而被以非 常短的氣流再導入,該電磁閥裝置(41)在此點進入(以某 速度)該真空室之Α氣上使這短氣流(每30秒大約每秒五 分之一)造成濃縮礦物及污泥在所謂晶體在它們形成時的 5 成晶點處排出,在依一般基準進行這項工作時,最後會限 制該排空流程之流動之晶體及/或污泥的形成措由該進料 水之排出濃度值來維持。 一直移除一百分比之由與該蒸發器之去水流程有關之 該進料控制閥所導入之水保持濃縮物係在不適合該熱交換 10 器及煮沸室結垢的一值。 對熟習此項技藝者而言可以輕易了解的是本發明提供 可以達到大範圍要求的一彈性系統,並且該系統可以藉由 適當程式化該π模糊π邏輯控制來獨特地修改而適用各安 裝。 15 這些應用可以單獨、互相、或一起工作的原因是由於 利用一程式化模糊邏輯系統藉電子控制所有前述功能得以 平衡各種流程。 決定各種流程之要求及藉由各種閥之電子裝置改變 (開關)的裝置係依據有關於特殊功能之狀態之電子程式要 20 求來完成。. 同時,監測、修正與維持在該蒸發室内之平衡,該等 電子設備可以偵測到開始夹帶並且關閉輸入該煮沸室之進 料水直到沸騰的溫度積體電路並且在該蒸發室内的平衡穩 定為止。當該進料水在上述條件下被關閉時,該單元將仍 第27頁 ^紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) -------------裝·-------訂---------線 (請先閱讀背面之注意事項再填寫本頁) 478948 A7 B7 五、發明說明(丨6 會產生出蒸餾水。 如前所述,所有的三種功能可以在同時或任兩者一 起、與任一或另一:者一起或由其自身來工作,該能量係機 械地協調的。 在不偏離本發明之情形下可對這些實施例進行各種改 變與修改。 10 15 ^--------^--------- (請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 20 第28頁 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) 478948 A7 B7 經濟部智慧財產局員工消費合作社印製 五、發明說明(α^7)1 .....煮沸室 2 .....冷凝室 3 .....加熱管. 5 4.....冷媒冷凝管 5 .....生水冷凝管 6 .....蒸餾水槽 7.. ...生水槽 8.....電磁閥裝置 1〇 9.....蒸餾水泵 10.. ..生水泵 11.. ..真空抽取裝置 12.. ..Τ-接頭 13.. ..流量控制閥 15 14....止逆閥 15.. ..真空抽取裝置 16.. ..導電度偵測器 17.. .. 3向電磁閥裝置 18.. ..抗垢管 20 19____濾網 20.. ..水位感應器 21____壓縮機 22.. ..電磁閥裝置 23.. ..電磁閥裝置 元件標號對照 24... .電磁閥裝置 25··· .防夾帶網 26··· .泡沫偵測器 26a.. .裙部 26b· · •井 27... .冷媒壓力調整器 28··· .熱水儲存槽 28a.. .溫度感應器 29··· .冷凝器 30··· .風扇 31··· .風扇 32··· •集液器 33... .乾燥器 34... .膨脹裝置 35... .止逆閥 36··· .文氏T型管 37.... ,膨脹裝置 38··· .膨脹裝置 39··· .冷卻管 40··· .冷卻管 41··· .電磁閥裝置 42··· .止逆閥 43... .電磁閥裝,置 第29頁 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐) » A -------------裝---------訂---------線 (請先閱讀背面之注意事項再填寫本頁) 478948 A7 B7 五、發明說明U1 ) 44.. ..溶劑槽 45.. ..冷藏/冰;東機 45a...溫度感應器 46.. ..電磁閥裝置 5 47____膨脹裝置 48.. ..感應計 49.. ..止逆閥 50.. ..空調機 5 0 a...溫度感應裔 10 51....電磁閥裝置 52.. ..膨脹裝置 53____感應計 54.. ..風扇 55. ^ 15 56....太陽能板 57.…·壓力控制器 58.. ..浮球 59.. ..電容測量裝置 60.. .·夾具 20 61.. ..執道引導構件 62.. ..軋道 63____框架 64.. ..握把 70.. ..熱交換器 71____排空清除系統 72.. ..熱交換器 73____冷凍抽吸管線 74.. ..風扇 75.…風扇 100.. .模糊邏輯電路 (請先閱讀背面之注意事項再填寫本頁) 第30頁 本紙張尺度適用中國國家標準(CNS)A4規格(210/ 297公釐)V. Description of the invention However, if conductivity is sensed when it is turned on after the time has elapsed. The solenoid valve (8) will remain closed and its cancellation each and every restart of this sensing is detected, for about 15 to 20 seconds until the boiling is stable and no entrainment (foam) is detected. When the conductivity is detected each time, the opening and closing time of the solenoid valve device does ensure that the solenoid valve device (8) does not vibrate in the polluted area, thereby preventing the valve from being worn out improperly. In the event of an overflow, or during severe boiling, another protection against pollution is a second conductive induction system with a detector similar to the main one, which instructs these electronic devices to exceed 2 to 5 Any one millionth of contaminated distilled water passes through the condensing chamber to drain the contaminated steamer water. Distilled water will only be directed back to the steaming tank (6) when the pollution level is, for example, less than 2 ppm, which will occur after the detection of steam storage water, such as seconds. When the method does not rely on measuring the conductivity in the storage tank 'it is more reliable than that method. Any contaminated distilled water passes through the 3 located between the distillation suction line and the outlet of the condensation chamber (2) and the vacuum extraction device (15), the distilled water pump (9) and the distilled water tank (6). The diversion solenoid valve device (π) is redirected to the raw water pump (10) delivery system and its raw water tank (7). If the pollution is detected by the detection system, the distilled water will be drained away from the distilled water suction pumping system composed of the vacuum extraction device (15), the distilled water pump (9) and the distilled water tank (6), so the distilled water Tank (6) is not contaminated. g. Another process to be considered is to prevent the formation of crystals at the discharge outlet. I 5 10 15 20 Page 26 This standard applies the Chinese national standard specifications. ⑵ X 公公 爱 ^ ---------- ------- ^ (Please read the notes on the back before filling out this page) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 478948 A7 B7_ V. Description of the invention (ΐψ), so that the atmosphere passes through a timer switch The solenoid valve device (41) is re-introduced with a very short airflow. At this point, the solenoid valve device (41) enters (at a certain speed) the A gas in the vacuum chamber to make this short airflow (about every 30 seconds approximately every One-fifth of a second) causes concentrated minerals and sludge to be discharged at 50% of the so-called crystals when they are formed. When this work is performed on a general basis, the flow of crystals and / Or the sludge formation measures are maintained by the discharge concentration value of the feed water. A percentage of the water retention concentrate introduced by the feed control valve associated with the dewatering process of the evaporator has been removed at a value that is not suitable for fouling of the heat exchanger and the boiling chamber. For those skilled in the art, it is easy to understand that the present invention provides a flexible system that can meet a wide range of requirements, and the system can be uniquely modified by appropriately programming the π fuzzy π logic control to suit each installation. 15 The reason these applications can work alone, with each other, or together is because of the use of a stylized fuzzy logic system to electronically control all the aforementioned functions to balance the various processes. The devices that determine the requirements of various processes and change (switch) by the electronic devices of various valves are based on electronic program requirements regarding the status of special functions. At the same time, to monitor, correct and maintain the balance in the evaporation chamber, these electronic devices can detect the temperature of the integrated circuit that starts entrainment and closes the feed water input to the boiling chamber until boiling and balance in the evaporation chamber. So far. When the feed water is turned off under the above conditions, the unit will still be on page 27. ^ The paper size applies the Chinese National Standard (CNS) A4 specification (210 X 297 mm) ----------- --Installation --------- Order --------- line (please read the precautions on the back before filling this page) 478948 A7 B7 V. Description of the invention (丨 6 will produce distilled water. As mentioned earlier, all three functions can work simultaneously, or both, with either or the other: the one or the other, the energy being mechanically coordinated. Without departing from the invention Various changes and modifications can be made to these embodiments. 10 15 ^ -------- ^ --------- (Please read the notes on the back before filling this page) Intellectual Property Bureau, Ministry of Economic Affairs Printed by Employee Consumer Cooperatives 20 Page 28 This paper size applies Chinese National Standard (CNS) A4 (210 X 297 mm) 478948 A7 B7 Printed by Employee Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs 5. Description of Invention (α ^ 7) 1 ..... Boiling chamber 2 ..... Condensing chamber 3 ..... Heating tube. 5 4 ..... Refrigerant condensing tube 5 ..... Raw water condensing tube 6 .... .Distilled water tank 7 ..... Raw water tank 8 ..... Solenoid valve device 10.9 ..... distilled water pump 10 ... raw water pump 11 .... vacuum extraction device 12 .... T-connector 13 ... flow control valve 15 14 .... Non-return valve 15 ... Vacuum extraction device 16 ... Conductivity detector 17 ... 3-way solenoid valve device 18 .... Anti-scale pipe 20 19____ strainer 20 ... Water level Sensor 21____ Compressor 22 ... Solenoid valve device 23 ... Solenoid valve device component number comparison 24 ... Solenoid valve device 25 ··. Anti-entrainment net 26 ··. Foam detector 26a ... skirt 26b ... well 27 ... refrigerant pressure regulator 28 ... hot water storage tank 28a ... temperature sensor 29 ... condenser 30 ... fan 31 ···· fan 32 ···· collector 33 ... .dryer 34 ... .expansion device 35 ... .check valve 36 · .. · Venturi T-tube 37 ... Expansion device 38 ... Expansion device 39 ... Cooling tube 40 ... Cooling tube 41 ... Solenoid valve device 42 ... Check valve 43 ... Page 29 This paper size is applicable to China National Standard (CNS) A4 (210 X 297 mm) »A ------------- Installation --------- Order- ------- (Please read the precautions on the back before filling this page) 478948 A7 B7 V. Description of the invention U1) 44.... Solvent tank 45... Refrigeration / ice; East machine 45a ... Temperature sensor 46. ... Solenoid valve device 5 47____ Expansion device 48 ... Inductive meter 49 ... Check valve 50 .... Air conditioner 5 0 a ... Temperature sensor 10 51 .... Solenoid valve Device 52 ... Expansion device 53____ Inductive meter 54 ... Fan 55. ^ 15 56 .... Solar panel 57 .... Pressure controller 58 ... Float 59 ... Capacitance measurement Device 60 ...... 20 .. 61 ... .. heat exchanger 73____ freezer suction line 74 ... fan 75 .. fan 100 .. fuzzy logic circuit (please read the precautions on the back before filling this page) page 30 This paper is for China National Standard (CNS) A4 Specification (210/297 mm)
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AUPP3641A AUPP364198A0 (en) | 1998-05-22 | 1998-05-22 | Various vacuum distillation equipment or the like |
PCT/AU1999/000203 WO1999061125A1 (en) | 1998-05-22 | 1999-03-24 | Hybrid distillation method and apparatus |
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ES2176126B1 (en) * | 2001-05-04 | 2004-02-01 | Serna Hermanos A A S L | INTEGRAL SYSTEM OF HEATING, REFRIGERATION AND PRODUCTION OF SANITARY HOT WATER THROUGH RECOVERY |
US6830661B1 (en) * | 2001-10-02 | 2004-12-14 | Environmental Technology Enterprises, L.L.C. | Point of use water purification method and apparatus |
FR2860987B1 (en) * | 2003-10-15 | 2006-02-24 | Cheng Ming Chou | MULTI-STEP PROCESS FOR DISTILLATION, COOLING AND VACUUM FREEZING |
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US10207935B2 (en) | 2016-01-31 | 2019-02-19 | Qatar Foundation For Education, Science And Community Development | Hybrid desalination system |
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IT202100013613A1 (en) * | 2021-05-25 | 2022-11-25 | 77 Vision Way Ltd | WATER DISTILLATION DEVICE |
CN115263518B (en) * | 2022-07-22 | 2023-07-25 | 珠海格力电器股份有限公司 | Engine cooling combined system and control method thereof |
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US4316774A (en) * | 1979-07-05 | 1982-02-23 | United Technologies Corporation | Thermoelectric integrated membrane evaporation system |
WO1988004193A1 (en) * | 1986-12-03 | 1988-06-16 | Hoffman Frank W | Liquid purification system |
US4770748A (en) * | 1987-02-24 | 1988-09-13 | Roncell, Inc. | Vacuum distillation system |
US6010599A (en) * | 1995-09-20 | 2000-01-04 | American Technologies Group, Inc. | Compact vacuum distillation device |
-
1998
- 1998-05-22 AU AUPP3641A patent/AUPP364198A0/en not_active Abandoned
-
1999
- 1999-03-24 WO PCT/AU1999/000203 patent/WO1999061125A1/en active Application Filing
- 1999-05-20 TW TW89127107A patent/TW478948B/en not_active IP Right Cessation
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AUPP364198A0 (en) | 1998-06-11 |
WO1999061125A1 (en) | 1999-12-02 |
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