TW201940222A - Water treatment device - Google Patents

Water treatment device Download PDF

Info

Publication number
TW201940222A
TW201940222A TW108105861A TW108105861A TW201940222A TW 201940222 A TW201940222 A TW 201940222A TW 108105861 A TW108105861 A TW 108105861A TW 108105861 A TW108105861 A TW 108105861A TW 201940222 A TW201940222 A TW 201940222A
Authority
TW
Taiwan
Prior art keywords
water
treatment device
pure water
series
water treatment
Prior art date
Application number
TW108105861A
Other languages
Chinese (zh)
Inventor
高松章吾
塚本和巳
Original Assignee
日商栗田工業股份有限公司
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 日商栗田工業股份有限公司 filed Critical 日商栗田工業股份有限公司
Publication of TW201940222A publication Critical patent/TW201940222A/en

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/08Apparatus therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/42Electrodialysis; Electro-osmosis ; Electro-ultrafiltration; Membrane capacitive deionization
    • B01D61/44Ion-selective electrodialysis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/42Electrodialysis; Electro-osmosis ; Electro-ultrafiltration; Membrane capacitive deionization
    • B01D61/44Ion-selective electrodialysis
    • B01D61/54Controlling or regulating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/58Multistep processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B63SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63HMARINE PROPULSION OR STEERING
    • B63H21/00Use of propulsion power plant or units on vessels
    • B63H21/38Apparatus or methods specially adapted for use on marine vessels, for handling power plant or unit liquids, e.g. lubricants, coolants, fuels or the like
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B63SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63JAUXILIARIES ON VESSELS
    • B63J2/00Arrangements of ventilation, heating, cooling, or air-conditioning
    • B63J2/12Heating; Cooling
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/42Treatment of water, waste water, or sewage by ion-exchange
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/44Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/469Treatment of water, waste water, or sewage by electrochemical methods by electrochemical separation, e.g. by electro-osmosis, electrodialysis, electrophoresis

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Organic Chemistry (AREA)
  • Environmental & Geological Engineering (AREA)
  • Hydrology & Water Resources (AREA)
  • Mechanical Engineering (AREA)
  • Urology & Nephrology (AREA)
  • Combustion & Propulsion (AREA)
  • Ocean & Marine Engineering (AREA)
  • Nanotechnology (AREA)
  • General Chemical & Material Sciences (AREA)
  • Electrochemistry (AREA)
  • Molecular Biology (AREA)
  • Analytical Chemistry (AREA)
  • Water Treatment By Electricity Or Magnetism (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Treatment Of Water By Ion Exchange (AREA)

Abstract

According to the present invention, a portion of fresh water in a fresh water tank 1 is used as supply water for a low-pressure boiler or a middle-pressure boiler. The fresh water in the fresh water tank 1 is supplied to an RO device 6 via a pipe 2, a valve 3, a water supply pump 4, and an MF film device 5, which constitute a main line. The water that has passed through the RO device 6 is supplied to an electrical deionization device 11. An auxiliary line 20 is configured to produce pure water by allowing the fresh water from the fresh water tank 1 to pass through an MF film device 25 by means of a pipeline 21, a valve 22, and a water supply pump 24 and by allowing MF filtrate water to pass through an ion exchange resin device 26 to be deionized. When an abnormality occurs in the device, data on a component which has caused the abnormality is transmitted to a management department.

Description

水處理裝置Water treatment device

本發明是有關於一種水處理裝置,特別是有關於一種適於船舶內的純水製造裝置的水處理裝置。The present invention relates to a water treatment device, and more particularly, to a water treatment device suitable for a pure water manufacturing device in a ship.

對於在海洋中航行的船舶而言,確保飲用水或生活用水等水是重要的。因此,船舶上大多搭載有由海水藉由蒸餾等而製造淡水的造水裝置。由造水裝置製造的淡水有時除了用作飲用水等以外亦用作鍋爐供水(專利文獻1)。For ships sailing in the ocean, it is important to secure water such as drinking water or domestic water. Therefore, many ships are equipped with a fresh water generator which produces fresh water from seawater by distillation or the like. The fresh water produced by a fresh water generator may be used as a boiler water supply in addition to drinking water etc. (patent document 1).

船內的鍋爐例如是用於如下用途。
(1)於輪機船(turbine boat)中,設置主鍋爐作為將過熱蒸汽供給於輪機的蒸汽產生裝置。
(2)於柴油船中,以燃料、潤滑油、冷卻清水的加熱、烹調、熱水供應、製熱等為目的而需要大量的蒸汽,為了補助柴油引擎而設置供給飽和蒸汽的輔助鍋爐。
(3)於液貨船中,設置用以供給氧濃度≦5%的鍋爐排氣(不燃性)作為用以將貨艙(cargo tank)內的揮發性氣體擠出的惰性氣體的鍋爐。
The boilers in ships are used for the following purposes, for example.
(1) In a turbine boat, a main boiler is provided as a steam generating device for supplying superheated steam to the turbine.
(2) In diesel ships, a large amount of steam is required for the purpose of heating, cooking, hot water supply, and heating of fuel, lubricating oil, and cooling water, and an auxiliary boiler for supplying saturated steam is provided to supplement diesel engines.
(3) In a liquid cargo tank, a boiler for supplying boiler exhaust gas (non-combustible) with an oxygen concentration of ≦ 5% is provided as a boiler for inert gas used to squeeze out a volatile gas in a cargo tank.

先前,於任一用途中均主要使用低壓鍋爐、中壓鍋爐作為船內鍋爐。此時,於使用淡水作為鍋爐供水時,淡水的水質導致運轉不良的情況少。Previously, low-pressure and medium-pressure boilers were mainly used as shipboard boilers in any application. At this time, when fresh water is used as the boiler water supply, poor operation of the fresh water due to poor water quality is rare.

輪機船需要主要利用鍋爐來製造用以使蒸汽輪機運行的蒸汽,鍋爐運行台數對燃料消耗率的影響大。因此,近年來正研究下述結構:使用高壓鍋爐作為鍋爐,利用一個高壓鍋爐使多個蒸汽輪機運行,由此減少鍋爐運行台數而實現燃料消耗率的改善。Turbine ships need to mainly use boilers to produce steam to run steam turbines, and the number of boilers running has a large effect on fuel consumption. For this reason, in recent years, research is being conducted on a structure in which a high-pressure boiler is used as a boiler, and a plurality of steam turbines are operated using one high-pressure boiler, thereby reducing the number of boilers to operate and improving the fuel consumption rate.

於使用高壓鍋爐作為船內鍋爐的情形時,鍋爐供水為高溫,故而水質差(例如腐蝕性)容易導致鍋爐的運轉不良。由於鍋爐成為運轉不良時的影響非常大,故而理想的是將鍋爐供水的水質由淡水進一步高度化,將經去鹽處理的純水用作鍋爐供水。In the case of using a high-pressure boiler as an on-board boiler, the boiler water supply is at a high temperature, so poor water quality (for example, corrosiveness) easily leads to poor operation of the boiler. Since the influence of a boiler malfunctioning is very large, it is ideal to further improve the water quality of the boiler water supply from fresh water, and use the pure water treated with desalination as the boiler water supply.

關於鍋爐用純水製造裝置,已知串聯設置有超濾(Ultrafilter,UF)膜裝置、逆滲透(Reverse Osmosis,RO)裝置及電氣膜離子而成的裝置(專利文獻2)。Regarding a boiler pure water production device, it is known to install an ultrafiltration (UF) membrane device, a reverse osmosis (RO) device, and an electrical membrane ion device in series (Patent Document 2).

[專利文獻1]日本專利特開2007-132227號公報
[專利文獻2]日本專利特開2003-136065號公報
[Patent Document 1] Japanese Patent Laid-Open No. 2007-132227
[Patent Document 2] Japanese Patent Laid-Open No. 2003-136065

通常的情形時,於船內並未保管更換部件,故而即便於航行中純水製造裝置因部件的劣化、損傷、堵塞等而運轉變得不正常,亦無法更換部件,無法消除不正常。Under normal circumstances, replacement parts are not stored in the ship. Therefore, even if the pure water production device during the navigation becomes abnormal due to the deterioration, damage, or blockage of the parts, the parts cannot be replaced and the abnormality cannot be eliminated.

本發明的目的在於提供一種用以消除不正常的更換部件的獲取容易的水處理裝置。An object of the present invention is to provide a water treatment device that can easily obtain an abnormal replacement part.

本發明的水處理裝置對被處理水進行處理而製成處理水,其包括:發送機構,於該水處理裝置產生不正常時,將成為不正常原因的部件發送至管理部門或配送部門。The water treatment device of the present invention processes the water to be treated to produce treated water, and includes a sending mechanism, and when the water treatment device generates an abnormality, sends a component that causes the abnormality to a management department or a distribution department.

本發明的一態樣的水處理裝置中,所述水處理裝置為至少藉由RO裝置或RO裝置與電去離子裝置對被處理水進行處理而製造純水的純水製造裝置。In one aspect of the water treatment device of the present invention, the water treatment device is a pure water production device that processes pure water by at least an RO device or an RO device and an electric deionization device.

本發明的一態樣的水處理裝置中,所述水處理裝置具有:主系列,至少利用所述RO裝置或RO裝置與電去離子裝置對被處理水進行處理而製造純水;及純水製造用的預備系列,相對於該主系列而可串聯或並聯地通水。In one aspect of the water treatment device of the present invention, the water treatment device has: a main series, at least the RO device or the RO device and the electric deionization device are used to process the treated water to produce pure water; and pure water The preliminary series for manufacturing can pass water in series or parallel to the main series.

本發明的一態樣的水處理裝置中,所述預備系列具有離子交換樹脂裝置。In one aspect of the water treatment device of the present invention, the preliminary series includes an ion exchange resin device.

本發明的一態樣的水處理裝置中,所述水處理裝置的不正常為來自所述純水製造裝置的純水的水量低於規定量,或來自純水製造裝置的純水的導電度或總有機碳量(Total Organic Carbon,TOC)值超過規定值。In one aspect of the water treatment device of the present invention, the abnormality of the water treatment device is that the amount of pure water from the pure water production device is lower than a predetermined amount, or the conductivity of the pure water from the pure water production device is abnormal. Or the total organic carbon (TOC) value exceeds the specified value.

本發明的一態樣的水處理裝置為船舶搭載用。
[發明的效果]
One aspect of the present invention is a water treatment device for ships.
[Effect of the invention]

搭載有本發明的水處理裝置的船舶即便於水處理裝置的性能降低或發生故障時,亦將成為不正常原因的部件發送至管理部門或配送部門,故而可於下一停靠港立即獲取更換部件並進行部件更換。Ships equipped with the water treatment device of the present invention send parts that are the cause of abnormality to the management department or distribution department even when the performance of the water treatment device is degraded or fails, so the replacement part can be immediately obtained at the next port of call. And replace parts.

本發明的一態樣的水處理裝置中,純水製造裝置包括預備系列,故而即便主系列的性能降低或主系列發生故障時,亦立即使預備系列動作,藉此可繼續進行良好水質的純水製造。In one aspect of the water treatment device of the present invention, the pure water production device includes a preparatory series, so even if the performance of the main series is degraded or the main series fails, the preparatory series is immediately actuated, whereby the pure water with good quality can be continued Made of water.

圖1表示作為實施形態的水處理裝置的純水製造裝置。FIG. 1 shows a pure water production apparatus as a water treatment apparatus according to an embodiment.

將對海水進行蒸餾所得的淡水導入至淡水槽1內。淡水槽1內的淡水的一部分被用作低壓鍋爐或中壓鍋爐的供水。淡水槽1內的淡水經由構成主系列10的配管2、閥3、供水泵4及精密過濾(Membrane Filter,MF)膜裝置5而向RO(逆滲透)裝置6供給。RO裝置6的濃縮水經由配管7而送回至淡水槽1,其一部分經由從配管7分歧的排放配管8及排放閥9而排出至系統外。Fresh water obtained by distilling seawater is introduced into the fresh water tank 1. A part of the fresh water in the fresh water tank 1 is used as a water supply for a low-pressure boiler or a medium-pressure boiler. The fresh water in the fresh water tank 1 is supplied to the RO (reverse osmosis) device 6 through a pipe 2, a valve 3, a water supply pump 4, and a precision filtration (Membrane Filter (MF)) membrane device 5 constituting the main series 10. The concentrated water of the RO device 6 is returned to the fresh water tank 1 through the pipe 7, and a part of the concentrated water is discharged to the outside of the system through the discharge pipe 8 and the discharge valve 9 branched from the pipe 7.

RO裝置6的透過水供給至電去離子裝置11。電去離子裝置11如專利文獻2所述,具有陰極及陽極、排列於該陰極與陽極之間的多個陽離子交換膜及陰離子交換膜、形成於該些膜彼此之間的濃縮室及去鹽室、填充至該去鹽室中的離子交換體、及對該陽極與陰極之間施加電壓的電源裝置。RO透過水於通過該去鹽室的期間中經去離子處理,成為純水。該純水經由配管12及閥13而取出一部分,用作高壓鍋爐等的供水。剩餘部分的純水經由配管15而向淡水槽1送回。電去離子裝置11的濃縮水經由配管16而送回至淡水槽1。The permeated water of the RO device 6 is supplied to the electric deionization device 11. As described in Patent Document 2, the electric deionization device 11 includes a cathode and an anode, a plurality of cation exchange membranes and anion exchange membranes arranged between the cathode and the anode, a concentration chamber formed between the membranes, and a desalination unit. A chamber, an ion exchanger filled in the desalination chamber, and a power supply device for applying a voltage between the anode and the cathode. The RO permeate water undergoes deionization treatment while passing through the desalination chamber, and becomes pure water. A part of this pure water is taken out through the piping 12 and the valve 13 and is used as water supply for a high-pressure boiler and the like. The remaining pure water is sent back to the fresh water tank 1 through a pipe 15. The concentrated water of the electric deionization device 11 is returned to the fresh water tank 1 through a pipe 16.

該純水製造裝置中,於產生來自電去離子裝置11的純水的水量少於規定值,或來自電去離子裝置11的純水的水質差(具體而言,例如導電度或TOC值高於規定值)等不正常時,藉由發送機構(例如衛星通信系統)將成為不正常原因的部件發送至管理部門的伺服器(server)。該伺服器以將該更換部件資訊及下一停靠港資訊(場所、時期)發送至更換部件供應部門(訂貨),而可於下一停靠港立即更換部件的方式預先籌備。In this pure water manufacturing apparatus, the amount of pure water generated from the electric deionization apparatus 11 is less than a predetermined value, or the pure water from the electric deionization apparatus 11 has poor water quality (specifically, for example, the conductivity or the TOC value is high). In the case of an abnormality such as a predetermined value), the sending mechanism (for example, a satellite communication system) sends a component that is the cause of the abnormality to a server of a management department. This server prepares in advance by sending the replacement part information and the next port information (location, time) to the replacement part supply department (ordering), and the parts can be replaced immediately at the next port.

參照圖2對另一實施形態進行說明。
該實施形態中,包括圖1所示的純水製造裝置作為主系列,並且與其不同而更包括預備系列20。
Another embodiment will be described with reference to FIG. 2.
In this embodiment, a pure water production apparatus shown in FIG. 1 is included as a main series, and a preliminary series 20 is further included.

預備系列20是以如下方式構成:藉由配管21、閥22、配管23及供水泵24使來自淡水槽1的淡水通水至MF膜裝置25,並使MF過濾水通水至離子交換樹脂裝置26而進行去離子處理,製造純水。來自預備系列20的純水從配管27經由閥29A、所述配管12、配管15而向淡水槽1送回,於使用時閥13打開,經由閥13而取出一部分。The preliminary series 20 is configured by passing fresh water from the fresh water tank 1 to the MF membrane device 25 through a pipe 21, a valve 22, a pipe 23, and a water supply pump 24, and passing MF filtered water to the ion exchange resin device. 26 and deionized to produce pure water. The pure water from the preliminary series 20 is returned from the piping 27 to the fresh water tank 1 through the valve 29A, the piping 12, and the piping 15, and the valve 13 is opened during use, and a part is taken out through the valve 13.

利用電阻率計、導電度計等感測器測量來自電去離子裝置11的純水的水質(電阻率或導電度等),並且利用流量感測器測量來自電去離子裝置11的純水流量,將該些感測器的檢測信號輸入至控制器(圖示省略)中。該控制器於以上的主系列10的運轉期間中,監視純水的水質及水量,於水質及水量的至少一者以既定期間以上低於設定值(水質差或水量少)的情形時,判斷為主系列10產生某些異常,如圖3所示,利用衛星通信系統等向純水製造裝置的管理部門通知異常,並且開始利用預備系列20的純水製造。另外,向管理部門通知更換部件。Sensors such as a resistivity meter and a conductivity meter are used to measure the water quality (resistivity or conductivity, etc.) of pure water from the electric deionization device 11, and a flow sensor is used to measure the pure water flow rate from the electric deionization device 11. , Input the detection signals of these sensors into the controller (not shown). This controller monitors the water quality and quantity of pure water during the operation period of the above main series 10, and judges when at least one of the water quality and quantity is lower than a set value (poor water quality or low water quantity) for a predetermined period or more. Some abnormalities are generated for the main series 10. As shown in FIG. 3, a satellite communication system or the like is used to notify the management department of the pure water production apparatus of the abnormality, and the pure water production of the preliminary series 20 is started. In addition, notify the management of replacement parts.

於使預備系列20動作的情形時,亦可停止主系列10而利用預備系列20來製造由純水製造裝置製造的純水的總量(關閉閥3、閥29B,打開閥22、閥29A,閥13僅於使用時打開),亦可使主系列10及預備系列20兩者動作,使來自主系列10的純水與來自預備系列20的純水合流並取出(關閉閥29B,打開閥3、閥22、閥29A,閥13僅於使用時打開)。When the pre-series 20 is operated, the main series 10 may be stopped and the pre-series 20 may be used to produce the total amount of pure water produced by the pure water manufacturing apparatus (close valve 3, valve 29B, open valve 22, valve 29A, The valve 13 is only opened during use), and both the main series 10 and the preparatory series 20 can be operated, so that the pure water from the main series 10 and the preparative series 20 merge and take out (close the valve 29B, open the valve 3 , Valve 22, valve 29A, valve 13 only open when in use).

所述說明的圖2中,將主系列10與預備系列20並聯設置,但亦可設置圖2中以兩點鏈線所示的串聯連接用配管30。於來自電去離子裝置11的純水的水量充分,但水質不良的情形時,將來自電去離子裝置11的純水通水至預備系列20而進行加工處理,經由配管27、配管12而取出良好水質的純水。In the illustrated FIG. 2, the main series 10 and the preliminary series 20 are provided in parallel, but a series connection pipe 30 shown by a two-point chain line in FIG. 2 may be provided. When the amount of pure water from the electric deionization device 11 is sufficient, but the water quality is poor, the pure water from the electric deionization device 11 is processed by passing water to the preparative series 20 and taken out through the pipes 27 and 12 Pure water with good water quality.

如此,與主系列10並聯或串聯地可通水地設置預備系列20,故而即便於主系列10產生了故障的情形時,亦可穩定地製造純水。另外,由於對高壓鍋爐穩定地供給純水,故而可使船舶航行至下一停靠港。In this way, the preparatory series 20 can be provided in parallel with or in series with the main series 10 so as to allow water to pass therethrough, so that even when a failure occurs in the main series 10, pure water can be stably produced. In addition, since the pure water is stably supplied to the high-pressure boiler, the ship can be sailed to the next port of call.

所述圖1、圖2的實施形態中,向預備系列20供給淡水槽1內的淡水的配管21直接連接於淡水槽1,但該配管21亦可自配管2分歧。In the embodiment shown in FIG. 1 and FIG. 2, the piping 21 for supplying fresh water in the fresh water tank 1 to the preliminary series 20 is directly connected to the fresh water tank 1, but the piping 21 may be diverged from the piping 2.

所述實施形態中使用MF膜裝置5,但亦可使用UF膜裝置。該些膜裝置亦可省略。圖1、圖2中,RO裝置6是以僅一段而圖示,但亦可設置為兩段以上。Although the MF membrane device 5 is used in the above embodiment, a UF membrane device may be used. These membrane devices can also be omitted. In FIG. 1 and FIG. 2, the RO device 6 is illustrated with only one segment, but it may be provided with two or more segments.

離子交換樹脂裝置26具有下述特徵:省空間;啟動快;可耐受原水水質的變動;維護作業簡易或不需要等。離子交換樹脂裝置與電去離子裝置等相比,雖然直至失效為止的壽命短,但只要可在到達下一停靠港之前僅以短期間穩定地進行去鹽處理即可,故而可於預備系列20中使用離子交換樹脂裝置。尤其為了實現由裝置的簡化所得的省空間化,較佳為設為非再生型的離子交換樹脂裝置。The ion exchange resin device 26 has the following characteristics: space saving; fast startup; resistance to changes in the quality of raw water; easy or unnecessary maintenance. The ion exchange resin device has a shorter lifespan than an electric deionization device, but as long as it can be desalted in a short period of time before reaching the next port of call, it can be used in the preparation series 20 An ion exchange resin device is used. In particular, in order to achieve space saving by simplifying the device, it is preferable to use a non-regeneration type ion exchange resin device.

離子交換樹脂裝置僅配置一塔或將兩塔串聯配置即可。兩塔的情形時,可採用陽離子交換→陰離子交換、陰離子交換→陽離子交換、陰離子-陽離子混合→陰離子-陽離子混合等各種組合。另外,亦可藉由下述方式而以一塔進行陽離子交換、陰離子交換的二段處理:於塔內以層狀態填充陽離子交換樹脂與陰離子交換樹脂的方式;或於塔內利用水平遮水板區分為上室、下室,並且設置從上室排水而導入至下室的配管的方式等。The ion exchange resin device may be configured with only one tower or two towers in series. In the case of two towers, various combinations such as cation exchange → anion exchange, anion exchange → cation exchange, anion-cation mixing → anion-cation mixing can be used. In addition, two stages of cation exchange and anion exchange can be performed in one tower by: filling the cation exchange resin and anion exchange resin in a layer state in the tower; or using a horizontal baffle plate in the tower It is divided into an upper chamber and a lower chamber, and a method of piping that drains water from the upper chamber and is introduced into the lower chamber is provided.

於要求更穩定處理的情形時,較佳為如圖2所示,於預備系列中藉由MF膜裝置25或UF膜裝置等進行膜過濾處理。When a more stable process is required, it is preferable to perform the membrane filtration process by the MF membrane device 25 or the UF membrane device in the preliminary series as shown in FIG. 2.

藉由如此般設置與主系列10不同的去除機制的預備系列20,亦有能避免由與主系列相同的原因所致的故障等優點。By providing the preliminary series 20 with a removal mechanism different from that of the main series 10 as described above, there are also advantages such that failure due to the same reason as the main series can be avoided.

圖2的情形時,主系列10正常運轉的期間中,預備系列20亦可基本上不用於去鹽而以浸漬狀態停止通水,但為了抑制細菌的產生,且於切換後可立即採水,較佳為使用配管28於預備系列20內使水循環而待機(standby)(關閉閥22、閥29A,打開閥3、閥29B,閥13僅於使用時打開)。於該情形時,擔心預備系列內的水溫的上升(超過50℃)或來自離子交換樹脂的溶出有機物的蓄積,故而較佳為定期向系統外排放等以使水溫或水質成為既定範圍內的方式進行控制。另外,若使來自配管28的回水回到淡水槽1,則會帶入溶解有大氣中的CO2 的水而對離子交換樹脂施加負荷,故而較佳為送回至配管23。In the situation shown in FIG. 2, during the normal operation of the main series 10, the pre-series 20 may be stopped in the immersion state without being used for desalting. However, in order to suppress the generation of bacteria, water can be collected immediately after switching. It is preferable to use a pipe 28 to circulate water in the standby series 20 and stand by (close the valve 22, the valve 29A, open the valve 3, the valve 29B, and open the valve 13 only when in use). In this case, it is feared that the temperature of the water in the preliminary series will rise (over 50 ° C) or the accumulation of dissolved organic matter from the ion exchange resin. Therefore, it is preferable to periodically discharge the water outside the system to keep the water temperature or water quality within a predetermined range Way to control. In addition, if the return water from the pipe 28 is returned to the fresh water tank 1, the water in which CO 2 in the atmosphere is dissolved will be taken to load the ion exchange resin, and therefore it is preferably returned to the pipe 23.

所述說明中,作為純水製造裝置的不正常現象,表示了純水的水量與導電度或TOC值,但不正常現象亦可例示RO裝置的壓損的過度上升、純水的水溫的過度上升等。In the description, the abnormal amount of pure water production equipment shows the amount of water and conductivity or TOC value of the pure water, but the abnormal phenomenon can also exemplify the excessive increase in pressure loss of the RO device, and the temperature of the pure water. Excessive rise and so on.

所述控制器的資料庫(database)中,登記有該些水量、導電度、壓損、水溫、TOC濃度等的基準值,並且登記有導致產生各測定值超過基準值的不正常現象的部件。於產生不正常現象時,將引起不正常現象的部件發送至管理部門。In the database of the controller, reference values of the water amount, conductivity, pressure loss, water temperature, TOC concentration, etc. are registered, and abnormalities that cause each measurement value to exceed the reference value are registered. component. When abnormalities occur, send the parts that caused the abnormalities to the management department.

所述基準值或成為不正常原因的部件亦可登記於管理部門的伺服器。此時,向管理部門的伺服器發送所述各測定項目的資料,伺服器監視純水製造裝置。於現場中的純水製造裝置產生不正常的情形時,由該伺服器向更換部件供應部門發送訂貨資料。The reference value or a component that causes an abnormality may be registered in a server of a management department. At this time, the data of each measurement item is transmitted to the server of the management department, and the server monitors the pure water production device. When abnormal conditions occur in the pure water manufacturing equipment on the spot, the server sends ordering data to the replacement parts supply department.

本發明中,較佳為基於用以檢測所述各項目的各感測器的偵測結果來自動運算所需要的更換部件的候補,並發送至管理者終端。例如,藉由事先製作使偵測結果與更換部件的候補關聯的主機(master)而可自動運算。In the present invention, it is preferable to automatically calculate a candidate for a replacement part based on a detection result of each sensor for detecting the various items, and send it to a manager terminal. For example, it is possible to automatically calculate a master by associating detection results with candidates for replacement parts in advance.

使航行的船的各時間的位置、部件庫存的位置與配送目標停靠港的位置、預備系列的剩餘可運轉預測期間相關聯,自動運算從哪個庫存點配送至哪個停靠港為有效率,並將結果發送至管理者終端。It is efficient to correlate the position of each time of the sailing ship, the position of parts inventory, the position of the destination port of delivery, and the remaining operational forecast period of the preliminary series, and automatically calculate from which inventory point to which port of delivery. The results are sent to the manager terminal.

管理者根據該些結果而進行訂貨手續。The manager performs the order procedure based on these results.

若相較於配送至停靠港而以船配送至海上更為有效率,則有時亦選擇以船配送至海上而不配送至停靠港。If it is more efficient to ship to the sea than ship to the port of call, sometimes it is also chosen to ship to the sea instead of to the port of call.

圖3為依序進行通知及訂貨的流程,但亦可不經由通知而進行訂貨處理。例如,亦可自動決定所需要的更換部件,自動完成從配送方法的選定至訂貨手續,並將訂貨結果告知管理者。此時,管理者於庫存點的配送準備的同時進行內容確認、顧客認可等作為事後處理,藉此可實現應對期間的縮短。FIG. 3 is a flow of notification and ordering in order, but order processing may be performed without notification. For example, it is also possible to automatically determine the required replacement parts, automatically complete the selection from the distribution method to the order procedure, and inform the manager of the order result. At this time, the manager can perform content confirmation, customer approval, etc. as post-processing while preparing for delivery at the inventory point, thereby shortening the response period.

使用特定的態樣對本發明進行了詳細說明,但所屬技術領域中具有通常知識者明瞭,可於不偏離本發明的意圖及範圍的情況下進行各種變更。
本申請案是基於2018年3月23日提出申請的日本專利申請案2018-056365,將其所有內容藉由引用而援用。
Although the present invention has been described in detail using specific aspects, those skilled in the art will understand that various changes can be made without departing from the intention and scope of the present invention.
This application is based on Japanese Patent Application No. 2018-056365 filed on March 23, 2018, the entire contents of which are incorporated by reference.

1‧‧‧淡水槽1‧‧‧ fresh water tank

2、7、12、15、16、21、23、27、28‧‧‧配管 2, 7, 12, 15, 16, 21, 23, 27, 28‧‧‧ Piping

3、13、22、29A、29B‧‧‧閥 3, 13, 22, 29A, 29B‧‧‧ Valve

4、24‧‧‧供水泵 4, 24‧‧‧ water supply pump

5、25‧‧‧MF膜裝置 5.25‧‧‧MF membrane device

6‧‧‧RO裝置 6‧‧‧RO device

8‧‧‧排放配管 8‧‧‧ discharge piping

9‧‧‧排放閥 9‧‧‧ Drain valve

10‧‧‧主系列 10‧‧‧Main Series

11‧‧‧電去離子裝置 11‧‧‧Electric deionization device

18‧‧‧黏泥控制劑添加裝置 18‧‧‧ slime control agent adding device

20‧‧‧預備系列 20‧‧‧Preparation Series

26‧‧‧離子交換樹脂裝置 26‧‧‧Ion exchange resin device

30‧‧‧串聯連接用配管 30‧‧‧Pipe for series connection

圖1為實施形態的純水製造裝置的構成圖。FIG. 1 is a configuration diagram of a pure water producing apparatus according to the embodiment.

圖2為另一實施形態的純水製造裝置的構成圖。 FIG. 2 is a configuration diagram of a pure water producing apparatus according to another embodiment.

圖3為實施形態的純水製造裝置的流程圖。 FIG. 3 is a flowchart of the pure water production apparatus of the embodiment.

Claims (6)

一種水處理裝置,對被處理水進行處理而製成處理水,其特徵在於包括:發送機構,於所述水處理裝置產生不正常時,將成為不正常原因的部件發送至管理部門或配送部門。A water treatment device for treating treated water to produce treated water, comprising: a sending mechanism that sends a component that becomes a cause of abnormality to a management department or a distribution department when the water treatment device is abnormal. . 如申請專利範圍第1項所述的水處理裝置,其中所述水處理裝置為至少藉由逆滲透裝置或逆滲透裝置與電去離子裝置對被處理水進行處理而製造純水的純水製造裝置。The water treatment device according to item 1 of the scope of patent application, wherein the water treatment device is a pure water manufacturing device that produces pure water by treating at least the treated water with a reverse osmosis device or a reverse osmosis device and an electric deionization device. Device. 如申請專利範圍第2項所述的水處理裝置,其中所述水處理裝置含有:主系列,至少利用所述逆滲透裝置或逆滲透裝置與電去離子裝置對被處理水進行處理而製造純水;及純水製造用的預備系列,相對於所述主系列而能夠串聯或並聯地通水。The water treatment device according to item 2 of the scope of patent application, wherein the water treatment device contains: a main series, at least the reverse osmosis device or the reverse osmosis device and the electric deionization device are used to process the treated water to produce pure water. Water; and a preliminary series for the production of pure water, which can pass water in series or parallel to the main series. 如申請專利範圍第3項所述的水處理裝置,其中所述預備系列具有離子交換樹脂裝置。The water treatment device according to item 3 of the patent application scope, wherein the preliminary series has an ion exchange resin device. 如申請專利範圍第2項至第4項中任一項所述的水處理裝置,其中所述水處理裝置的不正常為來自所述純水製造裝置的純水的水量低於規定量,或來自純水製造裝置的純水的導電度或總有機碳量值超過規定值。The water treatment device according to any one of items 2 to 4 in the scope of the patent application, wherein the abnormality of the water treatment device is that the amount of pure water from the pure water manufacturing device is less than a prescribed amount, or The conductivity or the total organic carbon value of the pure water from the pure water production device exceeds a predetermined value. 如申請專利範圍第1項至第5項中任一項所述的水處理裝置,其為船舶搭載用。The water treatment device according to any one of claims 1 to 5 of the scope of application for a patent, which is for use on a ship.
TW108105861A 2018-03-23 2019-02-21 Water treatment device TW201940222A (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2018-056365 2018-03-23
JP2018056365A JP6562106B1 (en) 2018-03-23 2018-03-23 Water treatment equipment

Publications (1)

Publication Number Publication Date
TW201940222A true TW201940222A (en) 2019-10-16

Family

ID=67690451

Family Applications (1)

Application Number Title Priority Date Filing Date
TW108105861A TW201940222A (en) 2018-03-23 2019-02-21 Water treatment device

Country Status (3)

Country Link
JP (1) JP6562106B1 (en)
TW (1) TW201940222A (en)
WO (1) WO2019181252A1 (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113402082A (en) * 2020-03-16 2021-09-17 佛山市云米电器科技有限公司 Household water purifying device
CN113402073A (en) * 2020-03-16 2021-09-17 佛山市云米电器科技有限公司 Household water purifying device
CN113493264A (en) * 2020-04-01 2021-10-12 佛山市云米电器科技有限公司 Household water purifying device
CN113493260A (en) * 2020-04-01 2021-10-12 佛山市云米电器科技有限公司 Household water purifying device
CN113493270A (en) * 2020-04-01 2021-10-12 佛山市云米电器科技有限公司 Household water purifying device

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60187383A (en) * 1984-03-05 1985-09-24 Kansai Electric Power Co Inc:The Process for preventing sticking of organism
JP3551048B2 (en) * 1998-12-03 2004-08-04 栗田工業株式会社 Operating method of ultrapure water production apparatus and ultrapure water production apparatus
JP2003114714A (en) * 2001-10-04 2003-04-18 Kurita Water Ind Ltd Facility management system
EP2208709A3 (en) * 2002-10-08 2011-03-09 Water Standard (CI), LP Mobile desalination plants and methods for producing desalinated water
JP4508701B2 (en) * 2004-04-05 2010-07-21 オルガノ株式会社 Water treatment system for electronic component parts manufacturing equipment
JP2006187719A (en) * 2005-01-06 2006-07-20 Toray Ind Inc Method for operating fresh water production device and fresh water production device
CH699530B1 (en) * 2005-03-07 2010-03-31 Klaus Kuhlgatz System and method for the holistic farming of ships.
JP5831327B2 (en) * 2012-03-28 2015-12-09 栗田工業株式会社 Remote monitoring device and remote monitoring method for ballast water treatment system
JP6399895B2 (en) * 2014-10-30 2018-10-03 株式会社日立製作所 Reverse osmosis treatment system and reverse osmosis treatment method
JP2017177050A (en) * 2016-03-31 2017-10-05 栗田工業株式会社 System for treating ship ballast water
JP6388020B2 (en) * 2016-12-12 2018-09-12 栗田工業株式会社 Ship equipment management system, equipment management program, and equipment management method

Also Published As

Publication number Publication date
JP2019166471A (en) 2019-10-03
JP6562106B1 (en) 2019-08-21
WO2019181252A1 (en) 2019-09-26

Similar Documents

Publication Publication Date Title
TW201940222A (en) Water treatment device
KR20140073312A (en) Apparatus for producing fresh water and electric power through forward osmosis, reverse osmosis and pressure retarded osmosis using treated sewage and seawater, and method for the same
US20150027937A1 (en) Seawater desalination system
JP2012192379A (en) Seawater desalination device and method for controlling the same
Zhang et al. Comparative techno-economic assessment of osmotically-assisted reverse osmosis and batch-operated vacuum-air-gap membrane distillation for high-salinity water desalination
Cardona et al. Energy saving in two-stage reverse osmosis systems coupled with ultrafiltration processes
Gude Thermal desalination of ballast water using onboard waste heat in marine industry
TW201940221A (en) Pure water producing device
CN105384205A (en) High conversion rate seawater desalination apparatus and use method thereof
TW201940432A (en) Pure water producing device
JP6562107B1 (en) Pure water production equipment
CN105565408A (en) Sea water desalination apparatus and usage thereof
JP2015117914A (en) Boiler system
JP5969355B2 (en) Nuclear fuel cooling method and nuclear fuel cooling device
JP7263730B2 (en) Boiler water treatment equipment and treatment method
JP6021739B2 (en) Boiler water supply system
CN110548548B (en) In-situ regeneration process and device for double-chamber ion exchanger and water treatment system
JP2008157579A (en) Make-up water supply method for boiler feed-water
JP7123250B2 (en) Ballast water treatment system and ship equipped with it
RU82215U1 (en) INSTALLATION FOR ELECTRIC DESALVATION OF A LIQUID OIL PRODUCT ARE ABLE TO USE AS A GAS TURBINE FUEL
Tyapkov Analysis of the Water Chemical Regime at an NPP with a VVER-1000 before and after Reconstruction of the Turbine Condenser’s Tube System
CN116854193A (en) Marine low-resin-consumption water quality treatment device and system
López García et al. Dow™ EDI modules perform well at bioenergy combines in Scandinavia
CN118183891A (en) Device for desalting sea water by RO and assisting in driving ship
JPH0579303A (en) Monitoring method and device where steam of condensed water circulation system flows