TWM559320U - Desalination system for salt water - Google Patents

Desalination system for salt water Download PDF

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Publication number
TWM559320U
TWM559320U TW106208200U TW106208200U TWM559320U TW M559320 U TWM559320 U TW M559320U TW 106208200 U TW106208200 U TW 106208200U TW 106208200 U TW106208200 U TW 106208200U TW M559320 U TWM559320 U TW M559320U
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Taiwan
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brine
fresh water
condensing device
temperature
pressure
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TW106208200U
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Chinese (zh)
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翁琳松
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金杰科技股份有限公司
翁琳松
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Priority to TW106208200U priority Critical patent/TWM559320U/en
Publication of TWM559320U publication Critical patent/TWM559320U/en

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Abstract

A desalination system for salt water, comprises a salt water nebulization device, nebulizing the salt water under normal temperature, so as to generate a mixed mist. A fresh water condensing device, coupled to the salt water nebulization device, condensing the mixed mist into the fresh water.

Description

鹽水淡化系統 Brine desalination system

本創作係關於一種鹽水淡化系統。 This creation is about a salt water desalination system.

地球上絕大部份的水是以海水的形式存在,約佔97%,然而海水為鹽水,無法做為飲用或灌溉用水,換言之,地球表面上自然存在的淡水僅佔3%,且大多以冰河形式存在,因此,將鹽水淡化為可用淡水的技術具有極大的應用需求。 The vast majority of the water on the earth is in the form of seawater, accounting for about 97%. However, seawater is salt water and cannot be used as drinking or irrigation water. In other words, fresh water naturally exists on the surface of the earth, accounting for only 3%. The form of glaciers exists, so the technology of desalinating brine to fresh water available has great application requirements.

現有的鹽水淡化技術主要分為蒸發法和薄膜法兩大類,蒸發法的基本原理是將鹽水加熱並收集蒸發後的水霧,包括多效蒸發法、多級閃化法和蒸氣壓縮法,但這種方式收集到的水霧仍會帶有少許鹽份;薄膜法主要有逆滲透法和電透析法兩種,基本原理是以半透膜過濾鹽水,使鹽水中的鹽離子被半透膜阻攔,通過半透膜的即為淡水,然而,鹽離子的尺寸很小,因此薄膜法需使用孔洞極小的半透膜,技術難度高,成本也高。 The existing desalination technology is mainly divided into two major categories: evaporation method and membrane method. The basic principle of evaporation method is to heat the brine and collect the water mist after evaporation, including multi-effect evaporation method, multi-stage flash method and vapor compression method, but The water mist collected in this way will still have a little salt; the membrane method mainly includes reverse osmosis method and electrodialysis method. The basic principle is to filter the salt water in the semi-permeable membrane so that the salt ions in the brine are semi-permeable membrane. Blocking, through the semi-permeable membrane is fresh water, however, the size of the salt ions is very small, so the thin film method requires the use of a semi-permeable membrane with a very small hole, which is technically difficult and costly.

本創作的另一目的之一,在於提出一種鹽水淡化系統。 One of the other purposes of this creation is to propose a brine desalination system.

根據本創作,一種鹽水淡化系統包括一鹽水霧化裝置,在常溫下將該鹽水霧化,以產生混合霧;以及一淡水凝結裝置,連接 該鹽水霧化裝置並接收該混合霧,用以從該混合霧中凝結出淡水。 According to the present invention, a brine desalination system includes a brine atomization device that atomizes the brine at a normal temperature to produce a mixed mist; and a fresh water condensation device that connects The brine atomizing device receives the mixed mist to condense fresh water from the mixed mist.

其中,該鹽水霧化裝置包括一加壓設備以及複數個噴霧嘴,或由複數個超音波震盪器實現。 Wherein, the salt water atomizing device comprises a pressing device and a plurality of spray nozzles, or is realized by a plurality of ultrasonic oscillators.

在一實施例中,該淡水凝結裝置包括一淡水冷凝裝置,以一第一溫度及第一壓力冷凝該混合霧,以收集淡水。較佳者,還包括一濃鹽水凝結裝置,包括一濃鹽水冷凝裝置,耦接該淡水冷凝裝置,以一第二溫度及第二壓力冷凝剩餘之混合霧;其中,該第一溫度與該第二溫度不同,該第一壓力與該第二壓力不同。 In one embodiment, the fresh water condensing device includes a fresh water condensing device that condenses the mixed mist at a first temperature and a first pressure to collect fresh water. Preferably, the method further comprises a concentrated brine condensing device, comprising a concentrated brine condensing device coupled to the fresh water condensing device to condense the remaining mixed mist at a second temperature and a second pressure; wherein the first temperature and the first The second pressure is different from the second pressure.

10‧‧‧鹽水霧化裝置 10‧‧‧Salt atomization device

11‧‧‧淡水凝結裝置 11‧‧‧ Freshwater condensation device

12‧‧‧濃鹽水凝結裝置 12‧‧‧Concentrated brine condensation device

22‧‧‧鹽水霧化裝置 22‧‧‧Salt atomization device

23‧‧‧風扇 23‧‧‧Fan

24‧‧‧淡水凝結裝置 24‧‧‧ Freshwater condensation device

242‧‧‧淡水冷凝裝置 242‧‧‧ Freshwater condensing unit

244‧‧‧淡水收集槽 244‧‧‧ Freshwater collection tank

25‧‧‧螺旋冷凝管 25‧‧‧Spiral condenser

26‧‧‧濃鹽水凝結裝置 26‧‧‧Concentrated brine condensation device

262‧‧‧濃鹽水冷凝裝置 262‧‧‧Concentrated brine condensing device

264‧‧‧濃鹽水收集槽 264‧‧‧Concentrated brine collection tank

301‧‧‧海水過濾裝置 301‧‧‧Seawater filtration device

302‧‧‧海水儲存槽 302‧‧‧Seawater storage tank

304‧‧‧海水加壓設備 304‧‧‧Seawater pressure equipment

305‧‧‧混合霧收集槽 305‧‧‧Mixed mist collection tank

510‧‧‧超音波震盪器 510‧‧‧Supersonic oscillator

520‧‧‧超音波震盪器 520‧‧‧Supersonic oscillator

第一圖為根據本創作之鹽水淡化系統一第一實施例的方塊圖;第二圖為根據本創作之鹽水淡化系統一第二實施例的方塊圖;第三圖為第二圖之實施例的細部架構圖;第四圖為根據本創作之鹽水淡化系統一第三實施例的方塊圖;第五圖為鹽水霧化裝置另一實施例的示意圖。 The first figure is a block diagram of a first embodiment of a brine desalination system according to the present invention; the second diagram is a block diagram of a second embodiment of a brine desalination system according to the present invention; and the third diagram is an embodiment of the second diagram. A detailed view of the fourth embodiment of the brine desalination system according to the present invention; and a fifth diagram of another embodiment of the saline atomization device.

第六圖為根據第四圖為根據本創作之鹽水淡化方法一實施例的流程圖。 The sixth figure is a flow chart of an embodiment of a brine desalination method according to the present invention according to the fourth figure.

第一圖為根據本創作之鹽水淡化系統一第一實施例的方塊圖,包括鹽水霧化裝置10、淡水凝結裝置11及濃鹽水凝結裝置 12。鹽水霧化裝置10在常溫下將鹽水霧化,以產生混合霧,接著,淡水凝結裝置11從該混合霧中凝結出淡水,並加以收集。較佳者,以濃鹽水凝結裝置12包括一螺旋冷凝管對已通過淡水凝結裝置11的剩餘霧進行第二次冷凝,以收集濃度較一開始輸入到系統裡的鹽水更高之濃鹽水。 The first figure is a block diagram of a first embodiment of a brine desalination system according to the present invention, including a salt water atomizing device 10, a fresh water condensing device 11 and a brine condensing device. 12. The salt water atomizing device 10 atomizes the salt water at a normal temperature to generate a mixed mist, and then the fresh water condensing device 11 condenses fresh water from the mixed mist and collects it. Preferably, the concentrated brine condensing unit 12 includes a spiral condenser for a second condensation of the remaining mist that has passed through the fresh water condensing unit 11 to collect a higher concentration of brine than the brine initially introduced into the system.

第二圖為根據本創作之鹽水淡化系統一第二實施例的方塊圖,包括鹽水霧化裝置22、淡水凝結裝置24以及鹽水凝結裝置26。在本實施例中,淡水凝結裝置24包括淡水冷凝裝置242、淡水收集槽244,鹽水凝結裝置26包括鹽水冷凝裝置262以及鹽水收集槽264。鹽水霧化裝置22產生之混合霧被輸送到淡水凝結裝置24後,由淡水冷凝裝置242以一第一溫度及一第一壓力,從該混合霧中冷凝出淡水並收集到淡水收集槽244;接著,剩餘的霧氣被輸送到鹽水冷凝裝置262,並被施加一第二溫度及一第二壓力,而凝結出高濃度的濃鹽水並收集到鹽水收集槽264。其中第一溫度與該第二溫度不同,且該第一壓力與該第二壓力不同,該第一溫度、第二溫度,第一壓力及該第二壓力之設定可參照露點溫度曲線做設計。 The second figure is a block diagram of a second embodiment of a brine desalination system according to the present invention, including a saline atomization device 22, a fresh water condensation device 24, and a brine condensation device 26. In the present embodiment, the fresh water condensing device 24 includes a fresh water condensing device 242, a fresh water collecting tank 244, and a brine condensing device 26 including a brine condensing device 262 and a brine collecting tank 264. After the mixed mist generated by the brine atomizing device 22 is sent to the fresh water condensing device 24, the fresh water condensing device 242 condenses the fresh water from the mixed mist at a first temperature and a first pressure and collects it into the fresh water collecting tank 244; The remaining mist is sent to the brine condensing device 262, and a second temperature and a second pressure are applied to condense a high concentration of concentrated brine and collect it into the brine collecting tank 264. The first temperature is different from the second temperature, and the first pressure is different from the second pressure, and the first temperature, the second temperature, the first pressure, and the second pressure are set according to a dew point temperature curve.

如第三圖所示,混合霧被風扇23吹送而送入淡水冷凝裝置242,淡水冷凝裝置242包括抽風機及冷凝管,當混合霧通過冷凝管時,淡水冷凝裝置242以第一溫度及第一壓力使淡水凝結,並儲存於淡水收集槽244。在淡水冷凝裝置24中未凝結的剩餘霧被吹送經螺旋冷凝管25而進入濃鹽水收集槽264,以第二溫度及第 二壓力凝結為濃鹽水,而最後未被冷凝的所有其他煙霧,則使其通過濃鹽水冷凝裝置262,其內設置有由金屬或其他不生鏽材質如塑膠所製的除霧網,讓尚未被冷凝之剩餘霧中的雜質被過濾下來,存積在濃鹽水收集槽264的濃鹽水中,使不致排入大氣中污染到空氣。如前所述,該第一溫度與該第二溫度不同,該第一壓力與該第二壓力不同。 As shown in the third figure, the mixed mist is blown by the fan 23 and sent to the fresh water condensing device 242. The fresh water condensing device 242 includes an exhaust fan and a condensing pipe. When the mixed mist passes through the condensing pipe, the fresh water condensing device 242 has the first temperature and the first temperature. A pressure causes the fresh water to condense and is stored in the fresh water collecting tank 244. The remaining uncondensed mist in the fresh water condensing device 24 is blown through the spiral condensing pipe 25 into the concentrated brine collecting tank 264 at the second temperature and the first The second pressure condenses into concentrated brine, and all other smoke that is not condensed at the end passes through the concentrated brine condensing device 262, which is provided with a defogging net made of metal or other non-rusting material such as plastic, so that The impurities in the remaining mist that have been condensed are filtered and stored in the concentrated brine of the brine collection tank 264 so that they are not discharged into the atmosphere and pollute the air. As previously mentioned, the first temperature is different from the second temperature, the first pressure being different from the second pressure.

第四圖是根據本創作之鹽水淡化系統一第三實施例的前段的方塊圖,在本實施例中,係以海水做為鹽水來源。如圖所示,進水口所提供之海水經海水過濾裝置301過濾後,儲存於海水儲存槽302,然後,使過濾後的海水流經海水加壓設備304加壓,再透過複數個細小的機械式噴霧嘴霧化成混合霧,並集中到混合霧收集槽305,其後,混合霧被進行前述之二階段式冷凝而分別收集成淡水及濃鹽水,在此不再重覆。 The fourth figure is a block diagram of the front section of a third embodiment of the brine desalination system according to the present invention. In the present embodiment, seawater is used as a source of brine. As shown in the figure, the seawater supplied from the water inlet is filtered by the seawater filtering device 301, stored in the seawater storage tank 302, and then the filtered seawater is pressurized by the seawater pressurizing device 304, and then passed through a plurality of fine machines. The spray nozzle is atomized into a mixed mist and concentrated in the mixed mist collecting tank 305. Thereafter, the mixed mist is subjected to the aforementioned two-stage condensation to be separately collected into fresh water and concentrated brine, and is not repeated here.

第五圖為根據本創作一第四實施例的示意圖,在本實施例中,霧化裝置包括超音波震盪器510及520,海水經超音波震盪器510及520震盪而霧化,再以風扇吹送而進行後續的淡水及濃鹽水冷凝收集程序。為簡化圖式,本實施例僅以兩個海水輸入口及超音波震盪器為例,每一海水輸入口可以設置多個超音波震盪裝置,在其他實施例中,海水輸入口的數量及超音波震盪器的數量皆可依實際需求增減。 The fifth figure is a schematic diagram of a fourth embodiment according to the present invention. In the embodiment, the atomizing device includes ultrasonic oscillators 510 and 520, and the seawater is oscillated and atomized by the ultrasonic oscillators 510 and 520, and then the fan is used. The subsequent fresh water and concentrated brine condensation collection procedures are carried out by blowing. In order to simplify the drawing, in this embodiment, only two seawater input ports and an ultrasonic oscillator are taken as an example, and each seawater input port may be provided with a plurality of ultrasonic oscillation devices. In other embodiments, the number of seawater input ports and the number of supersonic waves are exceeded. The number of sonic oscillators can be increased or decreased according to actual needs.

第六圖係根據本創作之鹽水淡化方法一實施例的流程圖,包括: 步驟S601:在常溫下霧化鹽水以產生混合霧;步驟S602:從該混合霧中凝結出淡水;以及步驟S603:從剩餘霧中凝結出濃鹽水 The sixth figure is a flow chart of an embodiment of a brine desalination method according to the present invention, comprising: Step S601: atomizing the brine at normal temperature to generate a mixed mist; step S602: condensing fresh water from the mixed mist; and step S603: condensing the concentrated brine from the remaining mist

各步驟的詳細操作皆已在前述實施例中敘明,因此不再重覆 The detailed operation of each step has been described in the foregoing embodiment, so it is not repeated

前述說明僅為教示,以使本創作所屬技術領域者得據以實施,然並不以此為限,本創作之權利範圍如後所宣告。 The foregoing description is only for the purpose of illustration, so that the technical field of the present invention can be implemented, and the scope of the present invention is not limited thereto.

Claims (5)

一種鹽水淡化系統,包括:一鹽水霧化裝置,在常溫下將該鹽水霧化,以產生混合霧;以及一淡水凝結裝置,連接該鹽水霧化裝置並接收該混合霧,用以從該混合霧中凝結出淡水。 A brine desalination system comprising: a brine atomization device that atomizes the brine at a normal temperature to generate a mixed mist; and a fresh water condensation device that connects the brine atomization device and receives the mixed mist for mixing from the mixture Fresh water condenses in the fog. 如申請專利範圍第1項之系統,其中該鹽水霧化裝置包括一加壓設備以及複數個噴霧嘴。 The system of claim 1, wherein the salt water atomizing device comprises a pressurizing device and a plurality of spray nozzles. 如申請專利範圍第1項之系統,其中該鹽水霧化裝置包括複數個超音波震盪器。 The system of claim 1, wherein the brine atomizing device comprises a plurality of ultrasonic oscillators. 如申請專利範圍第1項之系統,其中淡水凝結裝置包括:一淡水冷凝裝置,以一第一溫度及第一壓力冷凝該混合霧;以及一淡水收集槽,連接該淡水冷凝裝置,用以收集並儲存淡水。 The system of claim 1, wherein the fresh water condensing device comprises: a fresh water condensing device that condenses the mixed mist at a first temperature and a first pressure; and a fresh water collecting tank connected to the fresh water condensing device for collecting And store fresh water. 如申請專利範圍第4項之系統,更包括一濃鹽水凝結裝置,耦接該淡水凝結裝置,該濃鹽水凝結裝置包括:一濃鹽水冷凝裝置,耦接於該淡水冷凝裝置之後,以一第二溫度及第二壓力冷凝剩餘霧以凝結出濃鹽水;以及一濃鹽水收集槽,連接該濃鹽水冷凝裝置,用以收集並儲存該濃鹽水;其中,該第一溫度與該第二溫度不同,該第一壓力與該第二壓力不同。 The system of claim 4, further comprising a concentrated brine condensing device coupled to the fresh water condensing device, the concentrated brine condensing device comprising: a concentrated brine condensing device coupled to the fresh water condensing device The second temperature and the second pressure condense the remaining mist to condense the concentrated brine; and a concentrated brine collecting tank connected to the concentrated brine condensing device for collecting and storing the concentrated brine; wherein the first temperature is different from the second temperature The first pressure is different from the second pressure.
TW106208200U 2017-06-07 2017-06-07 Desalination system for salt water TWM559320U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113526762A (en) * 2021-06-16 2021-10-22 洛阳双瑞万基钛业有限公司 Method for treating high-salt-content wastewater by atomization method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113526762A (en) * 2021-06-16 2021-10-22 洛阳双瑞万基钛业有限公司 Method for treating high-salt-content wastewater by atomization method

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