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TW200819196A - Absorption freezing method to separate pure water from sea water - Google Patents

Absorption freezing method to separate pure water from sea water Download PDF

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Publication number
TW200819196A
TW200819196A TW95140125A TW95140125A TW200819196A TW 200819196 A TW200819196 A TW 200819196A TW 95140125 A TW95140125 A TW 95140125A TW 95140125 A TW95140125 A TW 95140125A TW 200819196 A TW200819196 A TW 200819196A
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Taiwan
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absorption
seawater desalination
patent application
desalination
refrigerant
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TW95140125A
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Chinese (zh)
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TWI303995B (en
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Ying-Chieh Liu
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Ying-Chieh Liu
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Publication of TWI303995B publication Critical patent/TWI303995B/en

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  • Sorption Type Refrigeration Machines (AREA)

Abstract

This investigation is to claim a purify method to separate pure water from sea water. Using absorption freezing mechanism, the pure water can be frozen independently. Re-used energy, exhaust heat and solar heat, as the input energy for the absorption freezing mechanism will provide less cost of the sea water purified process.

Description

200819196 九、發明說明: 【發明所屬之技術領域】 本發明有關吸收式冷;東海水淡化方法,利用 吸收式冷凍機的低辅助動力需求,及廢熱、太陽 能、地熱等再生能源做為熱源,提供冷媒具有冷 凍低溫條件,冷凍分離海水中的淡水及鹽分,達 到降低成本,推動海水淡化普及化之目的。 • 【先前技術】 最常運用於海水淡化方法,概約可分為非熱 處理法及熱處理法。非熱處理法包括逆滲透法及 電透析兩種’逆滲透法較適用於鹹水及海水脫 鹽;而電透析只適用於鹹水。熱處理法係以熱或 相變化,將液相先變為氣相(又稱蒸餾法)或固 相凍脫鹽(又稱冷凍法),再讓它回到液相,如此 即可將鹽份從水中分離,達到淡化的目的0 逆滲透法的主要成本為膜材及高壓能,必須 大幅降低膜材的成本,以利推廣。蒸德法盘冷壷 鲁 脫鹽法的優劣,^餾法的主要成本g蒸發所需的 熱能,熱效率較高;冷凍脫鹽法,關鍵在於冷凍 效能不如直接加熱式蒸餾法,除非能改善冷凍法 的^本。無論使用非熱處理法或熱處理法,截至 目前,海水淡化所需的成本不低,不利於普遍化 推展。 【發明内容】 經由理論能階分析,一般室溫下的海水,加 熱至蒸發狀態分離鹽分所需加諸的熱量,為冷凍 5 200819196 結冰後分離鹽分所需移除熱量的6倍’成本關鍵 為熱量外加及熱量移除的工具效能比較。冷凍法 ,需配合冷凍壓縮機及幫浦等輔助動力’能量轉 換效率較低,整體的效能不如直接加熱的蒸餾法 。本發明設計,採用吸收式冷凍機為主架構’儘 可能減少周邊支援裝備及辅助動力,提高海水淡 化之成本效能。 【實施方式】 茲謹就本發明「吸收式冷凍海水淡化法」的 内容,及其所產生的功效,配合圖式,舉出本案 之較佳實施例詳細說明如下。 請參閱「第一圖」所示,海水淡化槽5〇 , 由海水進口 5 1添加適量海水(或鹽水),槽内海 水的高度掩蓋冷媒管5 5,冷媒管内裝填冷媒, 冷媒可為濃鹽水,或添加防凍劑的溶液,以幫浦 30做為冷媒流動之辅助動力。冷媒管具有二個 支流,第一個冷凍支流5 6,整合於吸^式^象 機1 0的蒸發器1 4内,提供吸收式冷凍冷暮 發時所需的熱量,致使冷媒管第一支流的冷媒g =零度以下低溫條件。位於海水淡化槽的冷 目’其冷媒溫度低於海水凝固點,並於潘 = ;管的接觸表面產生冰結晶凝固並: f ’或稱為純水,達到分離海水鹽分的a = : ς 晶後,槽内底部的濃鹽水,ϊ 支流式心以 200819196 3熱交換器内,吸收冷凝器排放出的熱量,加速 融解海水淡化槽内的冰結晶。此時,可將第二海 水淡化槽的冷凍支流引入冷凍機蒸發器,進行第 一槽冷珠分離程序。第一槽融解後的純水,經由 3 5出口排出’完成海水淡化之程序。 本發明設計,以吸收式冷凍機做為海水淡化 冷凍脫鹽的冷凍工具,冷凍機的循環溶液,可為 氨水溶液、溴化鋰溶液等,第一圖所列範例為氨 水溶液之吸收式冷;東機。利用冷康機蒸發器的低 溫環境,可用於凍結海水中的淡水,分離海水中 的鹽分,並藉由冷凍機的冷凝器放出的熱量,加 速融解冰涞的淡水。本項發明亦可簡化為單段冷 凍脫鹽過程,或將冷媒管盤贴於製冰槽外殼,^ 製冰槽内的液體冷凍結冰。 吸收式冷涞機所需的熱源4 0,可直接利用 廢熱再生能源、太陽能、地熱等,或藉由生質能、 天然氣等燃料之加熱器,提供吸收式冷凍機操作 所需要之熱源。 θ 本發明設計的成本分析,若採用廢熱、太陽 能或地熱等再生利用能源,可節省熱能的成本; 再者,如以氨水溶液吸收式冷凍機,以氫氣(或氦 氣、氮氣)做為管路蓄壓源氣體,冷凍機的循環運 作幾乎不需外加辅助動力。海水淡化槽與冷象機 之間的冷媒循環操作,可藉由壓力幫浦做為加速 熱交換的辅助動力❹如此設計構造,可將海水淡 化的成本降至最低,達到普及化的目的。 综上所述,本發明的吸收式冷凍海水淡化 法’且利用再生能源,可有效降低海水淡化成本, 進而使本發明之産生能更實用、更符合使用者之 7 200819196200819196 IX. Description of the invention: [Technical field of the invention] The invention relates to absorption type cold; the method for desalination of the East Seawater utilizes the low auxiliary power demand of the absorption type refrigerator, and the renewable energy such as waste heat, solar energy and geothermal energy as a heat source, The refrigerant has the conditions of freezing and low temperature, and freezes and separates the fresh water and salt in the seawater to reduce the cost and promote the popularization of seawater desalination. • [Prior Art] The most commonly used method for seawater desalination can be divided into non-thermal treatment and heat treatment. Non-heat treatment methods include reverse osmosis and electrodialysis. The reverse osmosis method is more suitable for salt water and seawater desalting; while electrodialysis is only suitable for salt water. The heat treatment method changes the liquid phase to the gas phase (also known as distillation) or the solid phase freeze desalting (also known as freezing method) by heat or phase change, and then returns it to the liquid phase, so that the salt can be removed from the liquid phase. Separation in water to achieve the purpose of desalination 0 The main cost of reverse osmosis method is membrane and high pressure energy, and the cost of membrane material must be greatly reduced to facilitate the promotion. The advantages and disadvantages of the steam distillation method, the main cost of the distillation method, the thermal energy required for evaporation, and the high thermal efficiency; the key to the freezing desalination method is that the freezing performance is not as good as the direct heating distillation method, unless the freezing method can be improved. ^本. Regardless of whether non-heat treatment or heat treatment is used, the cost of seawater desalination is not low as of now, which is not conducive to generalization. SUMMARY OF THE INVENTION Through the theoretical energy level analysis, the seawater at room temperature is generally heated to the state of evaporation to separate the salt, and the heat required for the separation of salt is 6 times that is required for the separation of salt after icing. Comparison of tool performance for heat addition and heat removal. The freezing method needs to cooperate with the auxiliary power such as the refrigeration compressor and the pump. The energy conversion efficiency is low, and the overall efficiency is not as good as the direct heating distillation method. The design of the present invention uses an absorption chiller as the main structure to reduce the peripheral support equipment and auxiliary power as much as possible, and to improve the cost performance of seawater desalination. [Embodiment] The contents of the "absorption chilled seawater desalination method" of the present invention and the effects thereof are described in detail with reference to the drawings, and the preferred embodiments of the present invention are described in detail below. Please refer to the first figure, 5 海水 seawater desalination tank, add an appropriate amount of seawater (or salt water) from the seawater inlet 5 1 , the height of the seawater in the tank covers the refrigerant pipe 5 5 , the refrigerant pipe is filled with refrigerant, the refrigerant can be concentrated brine , or add antifreeze solution, with pump 30 as an auxiliary power for refrigerant flow. The refrigerant tube has two branches, and the first frozen branch stream 56 is integrated in the evaporator 14 of the suction type camera 10 to provide the heat required for the absorption type freezing cold burst, so that the refrigerant tube is first The tributary refrigerant g = low temperature conditions below zero. The cold head located in the desalination tank has a refrigerant temperature lower than the freezing point of seawater, and produces ice crystals on the contact surface of the tube; and f' or pure water, which reaches the separation of seawater salt a = : after crystal The concentrated brine at the bottom of the tank, 支 tributary heart in the heat exchanger of 200819196 3, absorbs the heat discharged from the condenser, accelerates the melting of ice crystals in the seawater desalination tank. At this point, the frozen substream of the second seawater desalination tank can be introduced into the freezer evaporator for the first tank cold bead separation procedure. The pure water melted in the first tank is discharged through the 3 5 outlet to complete the process of seawater desalination. The invention designs an absorption type freezer as a freezing tool for seawater desalination and freezing desalination, and the circulating solution of the refrigerator can be an ammonia aqueous solution, a lithium bromide solution, etc., the example shown in the first figure is an absorption type cold solution of an aqueous ammonia solution; . The low temperature environment of the cold-air evaporator can be used to freeze the fresh water in the seawater, separate the salt in the seawater, and accelerate the melting of the fresh water of the hail by the heat released by the condenser of the freezer. The invention can also be simplified as a single-stage freeze-free desalination process, or the refrigerant tube pan is attached to the ice-making tank casing, and the liquid in the ice tank is frozen and frozen. The heat source 40 required for the absorption type cold heading machine can directly use waste heat regeneration energy, solar energy, geothermal heat, etc., or provide a heat source for the operation of the absorption type refrigerator by using a heater such as biomass energy or natural gas. θ The cost analysis of the design of the invention can save the cost of heat energy by using waste heat, solar energy or geothermal energy, etc. Further, if the ammonia solution is used in an absorption type freezer, hydrogen (or helium or nitrogen) is used as a tube. The road accumulates the source gas, and the recirculating operation of the freezer requires almost no additional auxiliary power. The refrigerant circulation operation between the desalination tank and the cold camera can be designed by the pressure pump as an auxiliary power for accelerating heat exchange. The cost of desalination can be minimized and the purpose of popularization can be achieved. As described above, the absorption type chilled seawater desalination method of the present invention and the use of the renewable energy source can effectively reduce the seawater desalination cost, thereby making the production of the present invention more practical and more user-friendly 7 200819196

所須,確已符合發明專利申請之要件,爰 出專利申請。 凊提 惟以上所述者,僅為本發明之吸收式冷象海 水淡化設計較佳實施例而已,當不能以此限定本 發明實施之範故,凡依本發明申請專利範圍 及發明說明書内容所作之簡單的等效變化與修 飾’皆應仍屬本發明專利涵蓋之範圍内。It is necessary to meet the requirements of the invention patent application and to file a patent application. The above description is only for the preferred embodiment of the absorption cold-type seawater desalination design of the present invention, and it is not possible to limit the implementation of the present invention by this, and the content of the patent application and the contents of the invention are all made according to the present invention. Simple equivalent variations and modifications are still within the scope of the invention.

S 200819196 【圖式簡單說明】 第一圖:係本發明之吸收式冷凍海水淡化設計架 構示意圖。 【主要元件符號說明】 ίο吸收式冷凍機 11 —-發生器 12- 一分離器 13- 一冷凝器 14- 一蒸發器S 200819196 [Simplified description of the drawings] The first figure is a schematic diagram of the design structure of the absorption chilled seawater desalination of the present invention. [Main component symbol description] ίο absorption chiller 11 —-generator 12- one separator 13- one condenser 14-one evaporator

15- 一吸收器 21— -吸收式冷媒蒸汽+水 22— 吸收式冷媒蒸汽 23— —吸收式冷媒液體 24 ----吸收式冷媒+氫氣 25 ---氫氣 26 - 一濃吸收溶液 27-—稀吸收溶液 30-一幫浦 40---熱源 50---海水淡化槽 51-一海水進口 52 ---濃鹽水出口 53 ---淡水出口 55-一冷媒管 56 冷》東管路 57-一加溫管路 915- an absorber 21 - absorption refrigerant vapor + water 22 - absorption refrigerant vapor 23 - absorption refrigerant liquid 24 - absorption refrigerant + hydrogen 25 - hydrogen gas 26 - a concentrated absorption solution 27- - dilute absorption solution 30 - a pump 40 - heat source 50 - seawater desalination tank 51 - a seawater inlet 52 - - concentrated brine outlet 53 - freshwater outlet 55 - a refrigerant tube 56 cold "east pipeline 57-one heating pipe 9

Claims (1)

200819196 十、申請專利範園: 1、一種「吸收式冷凍海水淡化法」,利用吸收式 冷凍機為冷凍工具,藉由流經蒸發器的冷媒 管,回流至海水淡化槽,將海水(或鹽水)的溫 度降至凝固點以下,使得海水中的淡水(或稱 純水)產生冰結晶凝固,分離海水(或鹽水)中 的淡水及鹽分。 2、 如申請專利範圍第1項所述「吸收式冷凍海水 淡化法」,吸收式冷凍機做為海水淡化冷凍脫 鹽的冷凍工具,冷凍機的循環溶液,可為氨水 溶液、溴化鋰溶液等吸收式溶液。 3、 如申請專利範園第2項所述吸收式冷凍機,以 氨水溶液為吸收式溶液,可利用氫氣、氦氣, 或氮氣等氣體,做為管路蓄壓源氣體。 4、 如申請專利範圍第1項所述「吸收式冷凍海水 淡化法」,海水淡化槽内的冷媒管,可分別與 冷凍機蒸發器及冷凝器整合連結,提供海水淡 化程序所需的冷凍脫鹽及加速融解冰結晶之 溫度條件。 5、 如申請專利範圍第1項所述「吸收式冷凍海水 淡化法」,利用冷凍機的蒸發器與冷凝器操作 條件,可同時進行多組海水淡化槽的冷凍脫鹽 過程,及加速融解冰結晶過程。 6、 如申請專利範圍第1項所述「吸收式冷凍海水 淡化法j,海水淡化槽與冷凍機之間的冷媒 管’冷媒管内裝填冷媒,冷媒可為濃鹽水,或 添加防凍劑的溶液❹ 7、 如申請專利範圍第1項所述「吸收式冷凍海水 淡化法J,吸收式冷康機所需的熱量來源,可 10 200819196 直接利用廢熱、太陽能、地熱等再生能源,或 藉由生質能、天然氣等燃料之加熱器,做為吸 收式冷凍機操作所需要之熱源。 8、如申請專利範圍第1項所述「吸收式冷凍海水 淡化法」,亦可簡化為單段冷凍脫鹽過程,或 將冷媒管盤贴於製冰槽外殼,將製冰槽内的液 體冷凍結冰。200819196 X. Application for Patent Park: 1. An "absorption chilled seawater desalination method" in which an absorption chiller is used as a freezing tool, and the seawater (or brine) is returned to the desalination tank by a refrigerant pipe flowing through the evaporator. The temperature of the water drops below the freezing point, so that fresh water (or pure water) in the sea water is solidified by ice crystals, and the fresh water and salt in the seawater (or brine) are separated. 2. For the “absorption chilled seawater desalination method” mentioned in the first paragraph of the patent application, the absorption chiller is used as a freezing tool for seawater desalination and freezing desalination, and the circulating solution of the refrigerator can be an absorption system such as ammonia solution or lithium bromide solution. Solution. 3. If the absorption type freezer described in the second paragraph of the patent application park is used, the ammonia solution is used as the absorption solution, and the gas such as hydrogen, helium or nitrogen can be used as the pipeline pressure storage source gas. 4. For the “absorption chilled seawater desalination method” mentioned in the first paragraph of the patent application, the refrigerant pipes in the seawater desalination tank can be integrated with the chiller evaporator and condenser respectively to provide the required desalting desalination process. And accelerate the temperature conditions for melting ice crystals. 5. If the "absorption chilled seawater desalination method" mentioned in the first paragraph of the patent application scope uses the evaporator and condenser operating conditions of the refrigerator, the freezing desalination process of multiple sets of seawater desalination tanks can be simultaneously carried out, and the melting ice crystals can be accelerated. process. 6. As mentioned in the first paragraph of the patent application, “absorption chilled seawater desalination method j, refrigerant pipe between seawater desalination tank and freezer” is filled with refrigerant in the refrigerant pipe, and the refrigerant can be concentrated brine or a solution containing antifreeze ❹ 7. For the absorption chilled seawater desalination method referred to in the first paragraph of the patent application, the source of heat required for the absorption type cold-warming machine can be directly used by renewable energy such as waste heat, solar energy, geothermal energy, or by biomass. A heater for energy, natural gas, etc., as a heat source required for the operation of an absorption chiller. 8. The "absorption chilled seawater desalination method" described in item 1 of the patent application can also be simplified to a single-stage freeze desalination process. Or, the refrigerant tube is attached to the ice making tank casing, and the liquid in the ice making tank is frozen and frozen. 1111
TW95140125A 2006-10-30 2006-10-30 Absorption freezing method to separate pure water from sea water TWI303995B (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112791438A (en) * 2020-12-28 2021-05-14 魏永阳 Cold energy desalination system and process for treating salt water
CN114608217A (en) * 2022-03-14 2022-06-10 中南大学 Absorption refrigeration and seawater desalination system based on solar energy cascade utilization
CN115636864A (en) * 2022-11-18 2023-01-24 佛山中国发明成果转化研究院 Method for extracting protein by wall breaking of microalgae
CN116813011A (en) * 2023-03-03 2023-09-29 沈阳工程学院 Novel high-efficient sea water desalination system of brown gas heat reinforcement

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112791438A (en) * 2020-12-28 2021-05-14 魏永阳 Cold energy desalination system and process for treating salt water
CN114608217A (en) * 2022-03-14 2022-06-10 中南大学 Absorption refrigeration and seawater desalination system based on solar energy cascade utilization
CN115636864A (en) * 2022-11-18 2023-01-24 佛山中国发明成果转化研究院 Method for extracting protein by wall breaking of microalgae
CN116813011A (en) * 2023-03-03 2023-09-29 沈阳工程学院 Novel high-efficient sea water desalination system of brown gas heat reinforcement

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