JPH03181386A - Seawater desalting equipment - Google Patents
Seawater desalting equipmentInfo
- Publication number
- JPH03181386A JPH03181386A JP1324495A JP32449589A JPH03181386A JP H03181386 A JPH03181386 A JP H03181386A JP 1324495 A JP1324495 A JP 1324495A JP 32449589 A JP32449589 A JP 32449589A JP H03181386 A JPH03181386 A JP H03181386A
- Authority
- JP
- Japan
- Prior art keywords
- water
- reverse osmosis
- seawater
- cleaning
- pipe
- Prior art date
- Legal status (The legal status 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 status listed.)
- Pending
Links
- 239000013535 sea water Substances 0.000 title claims abstract description 37
- 238000011033 desalting Methods 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 116
- 239000000126 substance Substances 0.000 claims abstract description 31
- 239000007788 liquid Substances 0.000 claims abstract description 25
- 239000012190 activator Substances 0.000 claims abstract description 24
- 229910052500 inorganic mineral Inorganic materials 0.000 claims abstract description 10
- 239000011707 mineral Substances 0.000 claims abstract description 10
- 238000004140 cleaning Methods 0.000 claims description 66
- 238000001223 reverse osmosis Methods 0.000 claims description 47
- 239000003651 drinking water Substances 0.000 claims description 24
- 235000020188 drinking water Nutrition 0.000 claims description 24
- 239000002245 particle Substances 0.000 claims description 17
- 239000012528 membrane Substances 0.000 claims description 13
- 238000004519 manufacturing process Methods 0.000 claims description 12
- 238000010612 desalination reaction Methods 0.000 claims description 5
- 230000001954 sterilising effect Effects 0.000 claims description 2
- 239000000706 filtrate Substances 0.000 abstract description 4
- 238000005406 washing Methods 0.000 abstract 1
- 239000013505 freshwater Substances 0.000 description 13
- 241000894006 Bacteria Species 0.000 description 10
- 239000003814 drug Substances 0.000 description 8
- 229940079593 drug Drugs 0.000 description 8
- 230000000694 effects Effects 0.000 description 7
- 230000001105 regulatory effect Effects 0.000 description 6
- 235000014653 Carica parviflora Nutrition 0.000 description 5
- 241000243321 Cnidaria Species 0.000 description 5
- 229910052709 silver Inorganic materials 0.000 description 5
- 239000004332 silver Substances 0.000 description 5
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 4
- 230000000844 anti-bacterial effect Effects 0.000 description 4
- 239000000919 ceramic Substances 0.000 description 4
- 238000007689 inspection Methods 0.000 description 4
- 238000012423 maintenance Methods 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- 239000004575 stone Substances 0.000 description 4
- 230000007257 malfunction Effects 0.000 description 3
- 239000008213 purified water Substances 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- DWAQJAXMDSEUJJ-UHFFFAOYSA-M Sodium bisulfite Chemical compound [Na+].OS([O-])=O DWAQJAXMDSEUJJ-UHFFFAOYSA-M 0.000 description 2
- 244000052616 bacterial pathogen Species 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 2
- 239000000645 desinfectant Substances 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000000796 flavoring agent Substances 0.000 description 2
- 235000019634 flavors Nutrition 0.000 description 2
- 239000002778 food additive Substances 0.000 description 2
- 235000013373 food additive Nutrition 0.000 description 2
- 230000001089 mineralizing effect Effects 0.000 description 2
- 230000003204 osmotic effect Effects 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 235000010267 sodium hydrogen sulphite Nutrition 0.000 description 2
- 235000019640 taste Nutrition 0.000 description 2
- 230000009967 tasteless effect Effects 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 241000588724 Escherichia coli Species 0.000 description 1
- 241001544487 Macromiidae Species 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000035755 proliferation Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- -1 silver ions Chemical class 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 235000019583 umami taste Nutrition 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- 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
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Physical Water Treatments (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、海水淡水化装置に関し、大型ヨツトやクルー
ザー等の船舶、臨海地区や離島等の生活用水や飲料水が
確保しにくい状況下において好適に利用されるもので、
海水より淡水化した特に飲料水に適した純水を提供でき
るものである。[Detailed Description of the Invention] Industrial Application Field The present invention relates to a seawater desalination device, and is suitable for use in vessels such as large yachts and cruisers, and in situations where it is difficult to secure domestic water or drinking water, such as in coastal areas or remote islands. It is used,
It is possible to provide pure water that is desalinated from seawater and is particularly suitable for drinking water.
従来の技術及び本発明が解決しようとする課題従来、こ
の種の海水淡水化装置は種々提供されているが、いずれ
も装置が大型で保守・点検も容易でなく、蒸発型を採用
している場合は、大量のエネルギーを必要とし、コスト
高になる問題があった。Conventional Technology and Problems to be Solved by the Present Invention Conventionally, various seawater desalination devices of this type have been provided, but all of them are large and difficult to maintain and inspect, and they all use an evaporation type. In this case, there was a problem that a large amount of energy was required and the cost was high.
また、従来の装置は操作が複雑であり、例えば、海水か
ら淡水を造る造水時および、装置自体の洗浄時、その都
度手動により複数のコックを開閉し、確認した後で始動
しなければならず、誤動作による損傷の危険があった。In addition, conventional devices are complicated to operate; for example, when producing fresh water from seawater or cleaning the device itself, it is necessary to manually open and close multiple cocks each time and check before starting the device. However, there was a risk of damage due to malfunction.
しかも、この操作の繁雑な装置の洗浄を頻繁に行わなけ
れば、装置の耐久仕が急速に劣化する問題があった。Moreover, unless the equipment, which requires frequent cleaning, is not frequently cleaned, there is a problem in that the durability of the equipment rapidly deteriorates.
さらに、従来の装置では、海水から塩分、雑菌(細菌)
、バクテリア等を除去したろ過水は、H,0のみの純水
となっている。しかしながら、11tOのみの純水は、
飲料水としての基準はクリアするが、不純物等を除去す
ると同時にミネラル分も除去しているため、無味乾燥な
味で美味しい飲料水とはならない。かつ、自然に放置し
ていると雑菌が繁殖しやすく、飲料水取り出し口より雑
菌が配管内に侵入し増殖する危険がある。Furthermore, with conventional equipment, salt and bacteria (bacteria) are extracted from seawater.
Filtered water from which bacteria, etc. have been removed is pure water containing only H and 0. However, pure water with only 11tO is
Although it passes the standards for drinking water, since impurities and other minerals are removed at the same time, the water has a bland taste and is not delicious. Moreover, if left unattended, bacteria will easily breed, and there is a risk that bacteria will enter the pipes through the drinking water outlet and multiply.
本発明は、上記した種々の問題を解決せんとするもので
、装置自体が小型で耐久仕にも優れ、必要なエネルギー
を低減化し、しかも、造水及び洗浄操作をスイッチのオ
ン、オフ操作のみの簡単なものとし、さらに、ろ過水の
ミネラル化および滅菌化を図り、美味しく且つ雑菌が繁
殖しにくい飲料水を提供できるようにするものである。The present invention aims to solve the various problems mentioned above.The device itself is small and has excellent durability, reduces the required energy, and water generation and cleaning operations can be performed by simply turning on and off a switch. Furthermore, by mineralizing and sterilizing filtered water, it is possible to provide drinking water that is both delicious and resistant to the propagation of germs.
課題を解決するための手段
即ち、本発明は、導入される海水を半透膜を通過させて
純水にろ過する逆浸透式ろ過器と、ミネラル分を溶出す
る粒子および制菌作用を有する粒子等の複数種の粒子を
筒体内に充填して該筒体内部を通過するろ過水を活性化
する活性器と、薬剤タンクを備え、
上記逆浸透ろ過器の入水口をプランジャ・ポンプを介設
した配管に接続し、該配管を流路切替用の第1?II磁
弁を介して薬剤タンクに接続した洗浄液供給管と海水取
入管とに選択的に接続する一方、逆浸透式ろ過器の出水
口を流路切替用の第2電磁弁を介し上記活性器と薬剤タ
ンクに選択的に接続し、
かつ、上記プランジャ・ポンプをオン・オフ操作され造
水スイッチと洗浄スイッチとにより始動・停止されるモ
ータにより駆動させると共に、上記スイッチに上記電磁
弁等を連動させて造水・洗浄作動を自動制御するように
構成し、造水時には、造水および洗浄作動を逆浸透式ろ
過器に供給し、該ろ過器でろ過した水を活性器を通して
飲料水配管へ導出する一方、洗浄時にはろ過水を薬剤タ
ンクに導入して、設定量に達すると上記洗浄液供給管よ
り逆浸透式ろ過器へ循環させる構成としていることを特
徴とする海水淡水化装置を提供するものである。Means for Solving the Problems, that is, the present invention provides a reverse osmosis filter that filters introduced seawater through a semipermeable membrane into pure water, particles that elute minerals, and particles that have an antibacterial effect. It is equipped with an activator that fills a cylinder with multiple types of particles to activate the filtered water that passes through the cylinder, and a chemical tank, and a plunger pump is installed at the water inlet of the reverse osmosis filter. Connect the pipe to the first pipe for switching the flow path. It is selectively connected to the cleaning liquid supply pipe and the seawater intake pipe connected to the chemical tank through the II magnetic valve, while the water outlet of the reverse osmosis filter is connected to the above-mentioned activator through the second solenoid valve for flow path switching. and a chemical tank, and the plunger pump is driven by a motor that is turned on and off and started and stopped by a water production switch and a cleaning switch, and the solenoid valve, etc. is linked to the switch. The system is configured to automatically control water production and cleaning operations, and when producing fresh water, the water production and cleaning operations are supplied to a reverse osmosis filter, and the water filtered by the filter is passed through an activator to drinking water piping. To provide a seawater desalination device, characterized in that filtered water is introduced into a chemical tank during cleaning, and when a set amount is reached, it is circulated from the cleaning liquid supply pipe to a reverse osmosis type filter. It is.
本発明では、上記活性器を、上記逆浸透式ろ過器に連通
ずる入水口を一端に、飲料水配管に連通ずる出水口を他
端に設けた密閉式の筒体内に、純銀の焼結粒子と、超電
磁波セラミックスと同様の性能を打する自然石の粒子と
、造礁珊瑚を粒子にしたしの(コーラルサンド)とを混
合状態で充填した構成としており、該活性器を通過する
ろ過水に対して、上記粒子より溶出するミネラル分によ
りミネラル化すると共に、超電磁セラミックス作用およ
び純銀による制菌作用を付与し、飲料水にうま味と安全
性を与えることを特徴としている。In the present invention, the activator is housed in a sealed cylindrical body having a water inlet communicating with the reverse osmosis filter at one end and a water outlet communicating with the drinking water pipe at the other end. The structure is filled with a mixture of natural stone particles that have the same performance as ultra-electromagnetic ceramics, and coral sand, which is made from reef-building coral particles.The filtered water that passes through the activator is It is characterized in that it is mineralized by the minerals eluted from the particles, and also imparts a super-electromagnetic ceramic effect and an antibacterial effect due to pure silver, thereby imparting umami and safety to drinking water.
また−本発明では、逆浸透式ろ過器を造水運転終了毎に
自動的に洗浄すると共に、1日の運転終了後には薬剤を
用いて洗浄するようにしており、そのため、各造水運転
終了毎に洗浄用スイッチを押さなくても洗浄運転に自動
的に切り替わる一方、1日の運転終了後には洗浄用スイ
ッチを押して薬剤を用いた洗浄運転としている。即ち、
造水運転終了後に自動的に切替わる洗浄運転においては
、逆浸透式ろ過器でろ過されたろ過水を薬剤タンク内に
供給して貯溜し、該タンク内にろ過水が設定量たまると
オンするスイッチを設け、設定量たまると海水の取り入
れによるろ過水の造水を停止すると同時に、タンク内の
洗浄液を逆浸透式ろ過器に循環させて内部の半透膜等を
洗浄し、かつ、洗浄後の液は排出してタンク内の液が無
くなると自動的に洗浄運転が停止するようにしている。Furthermore, in the present invention, the reverse osmosis filter is automatically cleaned at the end of each fresh water generation operation, and is also cleaned using a chemical after each day's operation. The cleaning operation is automatically switched to without having to press the cleaning switch each time, while the cleaning operation using chemicals is started by pressing the cleaning switch after the day's operation is completed. That is,
In the cleaning operation, which automatically switches after the fresh water generation operation is completed, filtrate water that has been filtered by a reverse osmosis filter is supplied and stored in the chemical tank, and turns on when a set amount of filtrate has accumulated in the tank. A switch is installed, and when a set amount of seawater has accumulated, it stops producing filtered water by taking in seawater, and at the same time circulates the cleaning liquid in the tank to the reverse osmosis filter to clean the internal semipermeable membrane, etc. The cleaning operation is automatically stopped when the liquid in the tank is exhausted.
かつ、1日の運転終了後には、保守点検のために、上記
薬剤タンク内に一定の殺菌剤(重亜硫酸ナトリウム:食
品添加剤)を投入すると共に、洗浄運転のスイッチをオ
ンし、上記した洗浄運転と同様に、まず、海水を取り入
れて逆浸透式ろ過器でろ過し、該ろ過水を薬剤タンクに
貯溜して薬剤が溶けた薬剤洗浄液を作り、設定量溜まっ
た後に、該薬剤洗浄液を逆浸透式ろ過器に循環して薬剤
洗浄を行うようにしている。At the end of the day's operation, a certain disinfectant (sodium bisulfite: food additive) is poured into the chemical tank for maintenance and inspection, and the cleaning operation switch is turned on. Similar to the operation, first, seawater is taken in and filtered through a reverse osmosis filter, and the filtered water is stored in a chemical tank to create a chemical cleaning solution containing dissolved chemicals.After the set amount has accumulated, the chemical cleaning solution is reversely pumped. It circulates through the osmotic filter for chemical cleaning.
さらに、本発明では、逆浸透式ろ過器で生成されたろ過
水を活性器へ供給する第2ffi磁弁と、活性器との間
に、第3電磁弁を介設し、該第311磁弁より排水管へ
連通ずる配管を設け、使用前の自浄作用として、逆浸透
式ろ過器により造水された純水を一定時間排出して、よ
り安全度の高い飲料水を提供するようにしている。Furthermore, in the present invention, a third solenoid valve is interposed between the second ffi magnetic valve that supplies filtered water generated by the reverse osmosis filter to the activator and the activator, and the 311th magnetic valve Piping is installed that connects to the drain pipe, and as a self-cleaning action before use, purified water produced by a reverse osmosis filter is discharged for a certain period of time, providing safer drinking water. .
さらにまた、本発明では、マイコンで運転を制御してお
り、装置全体の回路をコントロールすると共に、造水運
転中に、何等かの原因で水圧が低下したり、モータや電
磁弁等が故障した時に、故障発生箇所を検知および表示
し、それに伴う全回路の遮断と復帰を行っている。さら
に、故障等の原因を取り除いた後、全回路を正常に復帰
させるためのリセットスイッチら備えている。Furthermore, in the present invention, the operation is controlled by a microcomputer, which controls the entire circuit of the device, and also prevents water pressure from decreasing for some reason or failure of the motor or solenoid valve during fresh water generation operation. At times, the location of a failure is detected and displayed, and all circuits are accordingly shut off and restored. Furthermore, it is equipped with a reset switch that allows all circuits to return to normal after the cause of the failure is removed.
作用
本発明は上記した構成としていることにより、造水およ
び洗浄時に1つのスイッチを押してオンするだけ良く、
他の作動は全て自動化されているため、操作が極めて簡
単て、誤動作を防止することが出来る。Operation The present invention has the above-mentioned configuration, so that all you have to do is press one switch to turn it on during water generation and cleaning.
All other operations are automated, making it extremely easy to operate and preventing malfunctions.
また、逆浸透式ろ過器の洗浄は各造水運転毎に自動的に
為されると共に、洗浄のみを行う場合らスイッチを押す
たけて薬剤を含んだ洗浄液により、必要な時間をかけて
自動的に行うことが出来る。In addition, the reverse osmosis filter is automatically cleaned after each freshwater generation operation, and if only cleaning is required, the cleaning solution containing chemicals is automatically applied over the necessary time by pressing the switch as many times as necessary. It can be done.
よって、逆浸透式ろ過器の半透膜から塩分、コロイドお
よび細菌等の汚染物質を除去する洗浄作業を手軽に行う
ことが出来、該半透膜の寿命を伸ばすことが出来る。Therefore, cleaning work to remove contaminants such as salt, colloids, and bacteria from the semipermeable membrane of the reverse osmosis filter can be easily performed, and the life of the semipermeable membrane can be extended.
ぎらに、上記ろ過器でろ過された純水は無味乾燥で雑菌
が繁殖しやすいが、活性器を通過させていることにより
、安全性に優れ、かつ、美味しいミネラルウォーターと
することが出来る。Furthermore, the pure water filtered through the filter is tasteless and prone to the growth of bacteria, but by passing it through an activator, it can be made into mineral water that is both excellent in safety and delicious.
実施例
以下、本発明を図面に示す実施例により詳細に説明する
。EXAMPLES Hereinafter, the present invention will be explained in detail with reference to examples shown in the drawings.
本装置の構成を示す第1図において、1は逆浸透式ろ過
器、2は活性器(アクティベーター)、3は薬剤タンク
、4は高圧−低圧に可変されるプランジャ・ポンプ、5
.6.7は三方口の流路切替用の第11第2および第3
電磁弁である。In FIG. 1 showing the configuration of this device, 1 is a reverse osmosis filter, 2 is an activator, 3 is a drug tank, 4 is a plunger pump that can be varied between high pressure and low pressure, 5
.. 6.7 is the 11th, 2nd and 3rd for switching the flow path of the three-way port.
It is a solenoid valve.
上記逆浸透式ろ過器lは、第2図に示す作動原理からな
るもので、入水01aより導入した濃厚溶酸(海水)側
に浸透圧Poより大きい圧力Pをかlすることにより、
浸透現象とは逆に溶媒(水分子)がarci−溶液側X
から半透膜100を通過して希薄溶液側Yに移動する原
理を利用している。上記半透膜100としては公知の植
物性セルロース等からなるものを用いており、該半透膜
+00を通過させることにより、導入された海水より塩
分、雑菌、バクテリア、金属類、有機および無機物など
の水分子以外のものを完全に分離して、H,Oのみの純
水が希薄溶液側Yへ導出される。該H,0のみの純水が
、逆浸透式ろ過器lの出水口tbより取り出されるよう
にしている。The above-mentioned reverse osmosis filter l has the operating principle shown in Fig. 2, and by applying a pressure P greater than the osmotic pressure Po to the concentrated molten acid (seawater) side introduced from the inlet water 01a,
Contrary to the osmosis phenomenon, the solvent (water molecules)
It utilizes the principle that the liquid passes through the semi-permeable membrane 100 and moves to the dilute solution side Y. The semipermeable membrane 100 is made of a known material such as vegetable cellulose, and by passing through the semipermeable membrane +00, salt, germs, bacteria, metals, organic and inorganic substances, etc. are removed from the introduced seawater. Everything other than water molecules is completely separated, and pure water containing only H and O is led to the dilute solution side Y. The pure water containing only H and 0 is taken out from the water outlet tb of the reverse osmosis filter l.
本実施例ではプランジャ・ポンプ4で55kg/C−に
圧縮された高圧水を入水口1aに圧送し、半透膜100
により透過された純水(HtO)は第1出水口tbより
送り出し、透過されない水は濃縮水となって第2出水口
1cより送り出して排出するようにしている。本逆浸透
式ろ過器lの性能は入水01aからの水量の30%がろ
過された純水として第1出水口1bより取り出され、第
2出水口1cより残りの70%を排出している。In this embodiment, high-pressure water compressed to 55 kg/C- is pumped to the water inlet 1a by the plunger pump 4, and the semi-permeable membrane 100
The purified water (HtO) that is permeated is sent out from the first water outlet tb, and the water that is not permeated becomes concentrated water and is sent out and discharged from the second water outlet 1c. The performance of this reverse osmosis type filter 1 is that 30% of the amount of water from the inlet water 01a is taken out as filtered pure water from the first water outlet 1b, and the remaining 70% is discharged from the second water outlet 1c.
上記活性器2は、上記逆浸透式ろ過器lで生成されたろ
過水(純水)を通過させることにより瞬時に活性化して
飲料水として適したものとするものである。該活性器2
は第3図に示すように、入水口2aを一端に、出水口2
bを他端に設けた筒体101内に、純銀の焼結粒子A1
超電磁波セラミックスと同様の性能を有する自然石の粒
子B1造礁珊瑚を粒子にしたもの(コーラルサンド)C
を混合状態で充填した構成としている。上記純銀の粒子
Aは水中で銀イオンを発生し、銀の持つ制菌作用により
、細菌の繁殖を防ぎ安全性の高い飲料水とする作用を有
する。上縁超電磁波セラミックスと同様の性能を有する
自然石の粒子Bは超電磁波により透過中の水を瞬時に活
性化する性能を有する。The activator 2 instantly activates the filtered water (pure water) produced by the reverse osmosis filter 1 by passing it therethrough, making it suitable for drinking water. The activator 2
As shown in Figure 3, the water inlet 2a is at one end and the water outlet 2
Pure silver sintered particles A1 are placed inside the cylinder 101 with b provided at the other end.
Particles of natural stone that have the same performance as superelectromagnetic ceramics B1 Particles made from reef-building coral (coral sand) C
The structure is such that it is filled in a mixed state. The pure silver particles A generate silver ions in water, and due to the antibacterial action of silver, they have the effect of preventing the proliferation of bacteria and making drinking water highly safe. The natural stone particles B, which have the same performance as the upper edge superelectromagnetic wave ceramics, have the ability to instantaneously activate the water being transmitted by superelectromagnetic waves.
ろ過水を活性化すると、腐敗しにくく、かつ、該活性化
された水は体内において老廃物を排せつし、活力を与え
て病気に対する抵抗力を強める作用を有する。かつ、該
自然石の粒子Bはミネラルを溶出し、ろ過水をミネラル
化する作用も有する。コーラルサンドからなる粒子Cも
炭酸カルシウム等のミネラル分を溶出し、ろ過水を弱ア
リカリ性の美味しいミネラルウォーターとする作用を有
する。When filtered water is activated, it is less likely to putrefy, and the activated water has the effect of excreting waste products from the body, giving vitality, and strengthening resistance to diseases. In addition, the natural stone particles B also have the effect of eluting minerals and mineralizing filtered water. Particles C made of coral sand also have the effect of eluting minerals such as calcium carbonate and turning filtered water into slightly alkaline and delicious mineral water.
上記した種々の作用を有する31]tの粒子A、B。Particles A and B of 31]t having the various effects described above.
Cを充填した筒体101を通過させることにより、3種
の相乗効果により、逆浸透式ろ過器lでろ過された純水
は瞬間的に活性化され、水にうま味と安全性が付与され
、飲料水に適した水となって該活性器2の出水口2bよ
り取り出されるようにしている。By passing through the cylindrical body 101 filled with C, the pure water filtered by the reverse osmosis filter l is instantaneously activated due to the synergistic effect of three types, imparting flavor and safety to the water. Water suitable for drinking is taken out from the water outlet 2b of the activator 2.
上記薬剤タンク3内には、1日の運転終了後、保守点検
するために、一定の殺菌剤(本実施例では、重亜硫酸ナ
トリウム二食品添加剤、純度65%で30g=0.15
ppm)からなる薬剤を投入し、上記逆浸透式ろ過61
から導入されるろ過水をタンク3内に導入して、上記薬
剤が溶けた洗浄液とし、該洗浄液を逆浸透式ろ過′a1
に循環させ、該ろ過器、特に半透膜lOOに付着した塩
分、コロイド、大腸菌などの汚染物質を自動的かつ迅速
に洗浄殺菌するようにしている。In the chemical tank 3, a certain disinfectant (in this example, sodium bisulfite and two food additives, 65% purity, 30 g = 0.15
ppm), and the above reverse osmosis filtration 61
The filtered water introduced from the tank 3 is introduced into the tank 3 to become a cleaning liquid in which the above-mentioned drug is dissolved, and the cleaning liquid is subjected to reverse osmosis filtration 'a1.
This system automatically and quickly cleans and sterilizes contaminants such as salts, colloids, and E. coli adhering to the filter, especially the semipermeable membrane 1OO.
上記逆浸透式ろ過器1は、その入水口1aを上記プラン
ジャ・ポンプ4を介して配管10の一端と接続し、該配
管IOの他端を3方口の流路切替用の第1ift磁弁5
と接続している。該第i?It磁弁5は海水取入管11
と接続すると共に、洗浄液供給管12と接続しており、
上記配管10を海水取入管11あるいは洗浄液供給管1
2と選択的に連通させている。海水取入管11は先端に
ストレーナ−13を取り付けていると共に、第1フイル
ター14、第2フイルター15を介設し、かつ、真空計
16を取り付けている。The reverse osmosis filter 1 has its water inlet 1a connected to one end of the piping 10 via the plunger pump 4, and the other end of the piping IO connected to a first ift magnetic valve for switching the three-way flow path. 5
is connected to. The ith? It magnetic valve 5 is seawater intake pipe 11
and is also connected to the cleaning liquid supply pipe 12,
The above piping 10 is connected to the seawater intake pipe 11 or the cleaning liquid supply pipe 1.
2 is selectively communicated with. The seawater intake pipe 11 has a strainer 13 attached to its tip, a first filter 14 and a second filter 15, and a vacuum gauge 16.
よって、造水時には上記プランジャ・ポンプ4を駆動す
ることにより海水取入管!!よりストレーナ−13、第
1および第2フイルター14.15を介して、第1′v
l磁弁5を通過したのち、配管IOより逆浸透式ろ過器
1に海水を取り入れている。Therefore, when producing fresh water, by driving the plunger pump 4, the seawater intake pipe! ! through the strainer 13 and the first and second filters 14.15.
After passing through the magnetic valve 5, the seawater is introduced into the reverse osmosis filter 1 through the pipe IO.
一方、洗浄時には、薬剤タンク3より洗浄液供給管12
を通して、第1電磁弁5を介して配管10より逆浸透式
ろ過器lに洗浄液を導入している。On the other hand, during cleaning, the cleaning liquid supply pipe 12 is connected to the chemical tank 3.
The cleaning liquid is introduced into the reverse osmosis type filter l from the pipe 10 through the first electromagnetic valve 5.
上記逆浸透式ろ過器Iは、その第1出水口1bを配管1
7の一端と接続し、該配管17の他端を3方口の流路切
替用の第2電磁弁6に接続している。該第2電磁弁6は
配管8、第3電磁弁7、配管18を介して活性器2に接
続すると共に、配管19を介して薬剤タンク3と接続し
ている。活性器2は上記した配管18と入水口2aを接
続すると共に、出水口2bを飲料水配管20に接続して
いる。よって、逆浸透式ろ過器lでろ過された純水は配
管17、第2電磁弁6、配管8、第3電磁弁7、配管I
8を通して活性化器2て活性化された後、飲料水配管2
0より飲料水として取り出すようにしている。また、洗
浄時には、逆浸透式ろ過器Iでろ過された純水を配管1
7、第2電磁弁6、配管19を介して薬剤タンク3に導
入している。該薬剤タンク3は、その入水口3aを配管
19と接続すると共に、第1出水口3bを上記洗浄液供
給管I2と接続し、かつ、第2出水口3cを排水管21
と接続している。排水管21は分岐点P1で分岐した排
水管22を介して逆浸透式ろ過器1の第2出水口1cと
接続している。また、排水管21からは、同様に、分岐
点Ptより配管23を分岐し、該配管23は上記の合流
点P3で上記排水管22と合流させている。該合流点P
、より下流位置に流路開閉用の第4電磁弁24および圧
力スイッチEを介設すると共に、合流点より上流端に圧
力計25を設置している。また、排水管22には上記合
流点P、より下流に調圧弁26を介設している。さらに
、排水管21には分岐点P4で分岐した排水管27を接
続し、該排水管27を上記第3電磁弁7と連通している
。The reverse osmosis filter I has its first water outlet 1b connected to the pipe 1.
7, and the other end of the pipe 17 is connected to a second electromagnetic valve 6 for switching three-way flow paths. The second electromagnetic valve 6 is connected to the activator 2 via a pipe 8, a third electromagnetic valve 7, and a pipe 18, and is also connected to the drug tank 3 via a pipe 19. The activator 2 connects the above-mentioned pipe 18 and the water inlet 2a, and also connects the water outlet 2b to the drinking water pipe 20. Therefore, the pure water filtered by the reverse osmosis filter l is transferred to the pipe 17, the second solenoid valve 6, the pipe 8, the third solenoid valve 7, and the pipe I.
After being activated by the activator 2 through 8, the drinking water pipe 2
The water is taken out as drinking water. Also, during cleaning, pure water filtered by reverse osmosis filter I is supplied to pipe 1.
7. The drug is introduced into the drug tank 3 via the second solenoid valve 6 and piping 19. The chemical tank 3 has its water inlet 3a connected to the pipe 19, its first water outlet 3b connected to the cleaning liquid supply pipe I2, and its second water outlet 3c connected to the drain pipe 21.
is connected to. The drain pipe 21 is connected to the second water outlet 1c of the reverse osmosis filter 1 via a drain pipe 22 branched at a branch point P1. Further, from the drain pipe 21, a pipe 23 is similarly branched from a branch point Pt, and the pipe 23 joins the drain pipe 22 at the above-mentioned merging point P3. The confluence point P
A fourth electromagnetic valve 24 for opening and closing the flow path and a pressure switch E are interposed at a downstream position, and a pressure gauge 25 is installed at an upstream end of the confluence point. Further, a pressure regulating valve 26 is provided in the drain pipe 22 at the confluence point P and further downstream. Further, a drain pipe 27 branched at a branch point P4 is connected to the drain pipe 21, and the drain pipe 27 is communicated with the third electromagnetic valve 7.
上記構造からなる本装置は、マイコンMで制御して自動
運転しており、使用者は、造水スイッチA(以下、メイ
ンスイッチAと称す)と洗浄スイッチBとをオン・オフ
操作するだけで、自動的に造水運転および洗浄運転され
るように構成している。This device, which has the above structure, is controlled by a microcomputer M and operates automatically, and the user only has to turn on and off the water generation switch A (hereinafter referred to as main switch A) and the cleaning switch B. The system is configured to automatically generate water and clean water.
即ち、逆浸透式ろ過器1へ海水あるいは洗浄液を供給す
るプランジャ・ポンプ4を駆動するモータ27は、オン
・オフ操作されるメインスイッチA1洗浄スイッチBに
接続され、これらのスイッチA、Bによりモータ27を
始動・停止して、プランジャ・ポンプ4を作動させてい
る。尚、該プランジャ・ポンプ4は造水運転中は調圧弁
26により高圧にセットされる一方、洗浄運転中には薬
剤タンク3にセットするスイッチCがオンすると同時に
第4電磁弁24はプランジャ・ポンプ4を低圧にセット
するように設定している。That is, the motor 27 that drives the plunger pump 4 that supplies seawater or cleaning liquid to the reverse osmosis filter 1 is connected to a main switch A1 and a cleaning switch B, which are operated on and off. 27 is started and stopped, and the plunger pump 4 is operated. The plunger pump 4 is set to a high pressure by the pressure regulating valve 26 during the fresh water production operation, while the fourth solenoid valve 24 is set to high pressure by the pressure regulating valve 26 during the cleaning operation when the switch C set in the chemical tank 3 is turned on. 4 is set to low pressure.
上記薬剤タンク3に取り付けるスイッチCは、タンクの
上端部近傍に設置し、洗浄液が所定量に溜まるとオンす
るようにしている。また、該スイッチCがオンすると、
第1電磁弁5が動作して配管10を洗浄液供給管I2と
連通させると共に第2電磁弁6が動作して配管17を配
管19と連通させ、かつ、第4電磁弁24が動作して流
路を開くようにしている。一方、薬剤タンク3内に水が
空に近い量に達すると、マイコンMはモータ27を停止
させ、かつ、電磁弁5.6.7.24が自動復帰される
ようにしている。即ち、第1電磁弁5は海水取入管11
を配管lOと連通し、第2f1!磁弁6は配管17と配
管8、第3電磁弁7を連通し、第4電磁弁24番上流路
を閉鎖し、調圧弁26はプランツヤ・ポンプ4を高圧に
制御する。尚、逆浸透式ろ過器lに接続される排水管2
3に介設する上記第4電磁弁24は固定圧力弁を有し、
作動すると自動的に圧力を5 kg/am’に設定する
ようにしている。A switch C attached to the chemical tank 3 is installed near the upper end of the tank, and is turned on when a predetermined amount of cleaning liquid has accumulated. Moreover, when the switch C is turned on,
The first solenoid valve 5 operates to communicate the pipe 10 with the cleaning liquid supply pipe I2, the second solenoid valve 6 operates to communicate the pipe 17 with the pipe 19, and the fourth solenoid valve 24 operates to communicate the pipe 10 with the cleaning liquid supply pipe I2. I'm trying to open the way. On the other hand, when the water in the chemical tank 3 reaches an almost empty amount, the microcomputer M stops the motor 27 and automatically returns the solenoid valves 5, 6, 7, and 24. That is, the first solenoid valve 5 is connected to the seawater intake pipe 11.
communicates with pipe lO, and the second f1! The magnetic valve 6 connects the pipe 17, the pipe 8, and the third solenoid valve 7, closes the upstream passage of the fourth solenoid valve 24, and the pressure regulating valve 26 controls the plantar pump 4 to a high pressure. In addition, the drain pipe 2 connected to the reverse osmosis filter l
The fourth electromagnetic valve 24 interposed in 3 has a fixed pressure valve,
When activated, the pressure is automatically set to 5 kg/am'.
次に、上記海水淡水化装置の作動について説明する。Next, the operation of the seawater desalination apparatus will be explained.
飲料水を得るための造水時、まず、メインスイッチAを
オンする。メインスイッチAがオンされるとモータ27
が駆動し、同時に第3電磁弁7が動作し、プランジャー
・ポンプ4を動作することにψより、ストレーナ−13
より海水取入管11に海水が取り入れられる。海水は第
1および第2フイルター14.15を通してごみを取り
、第1電磁弁5、配管10、プランジャー・ポンプ4を
経て、逆浸透式ろ過器!へ導入される。該ろ過器Iで純
水(H,O)となって出水口1bより取り出され、配管
17、第2電磁弁6、配管8を経て第3電磁弁7、排水
管2721を経て所要時間(約10分間)される。この
ように、飲料水の使用前の自浄作用として逆浸透式ろ過
器lにより造水された純水を所定時間排水して安全度の
高い飲料水を得るようにしている。When producing water to obtain drinking water, first turn on the main switch A. When main switch A is turned on, motor 27
is driven, the third solenoid valve 7 is operated at the same time, and the plunger pump 4 is operated.
Seawater is introduced into the seawater intake pipe 11. The seawater passes through the first and second filters 14 and 15 to remove debris, passes through the first solenoid valve 5, piping 10, plunger pump 4, and then is sent to a reverse osmosis filter! will be introduced to In the filter I, the pure water (H, O) is taken out from the water outlet 1b, passes through the pipe 17, the second solenoid valve 6, the pipe 8, the third solenoid valve 7, and the drain pipe 2721 for the required time (approx. 10 minutes). In this way, as a self-purification function of drinking water before use, the purified water produced by the reverse osmosis filter 1 is drained for a predetermined period of time to obtain highly safe drinking water.
上記した使用前の自浄作用が終了した後、第3電磁弁7
が自動的に切替わり、配管18を経て活性器2へろ過水
が導入される。活性器2を通過することによりミネラル
ウォーターとなると共に滅菌作用され、飲料水配管20
へ飲料水として取り出される。尚、該造水運転中は、プ
ランジャー・ポンプ4は55 kg/cmの高圧にセッ
トされて、海水を吸引している。逆浸透式ろ過器l内に
導入され、ろ過されない濃縮水は、第2出水口1cより
排水管22、調圧弁26を介して排水管21より排水さ
れる。造水運転を停止する場合は、メインスイッチAを
オフとすると自動的に後述する洗浄動作となり、洗浄が
終わると、4−夕27の駆動が停止し、本装置の運転が
停止される。After the self-cleaning action described above before use is completed, the third solenoid valve 7
is automatically switched, and filtered water is introduced into the activator 2 via the pipe 18. By passing through the activator 2, it becomes mineral water and is sterilized, and the drinking water pipe 20
It is extracted as drinking water. During the fresh water generation operation, the plunger pump 4 is set at a high pressure of 55 kg/cm to suck seawater. The unfiltered concentrated water introduced into the reverse osmosis filter 1 is drained from the second water outlet 1c through the drain pipe 22 and the pressure regulating valve 26, and then drained from the drain pipe 21. To stop the fresh water generation operation, turn off the main switch A, and the cleaning operation described later will automatically begin. When the cleaning is finished, the drive of the 4-7 27 will be stopped, and the operation of this device will be stopped.
上記した造水運転毎に行なわれる造水終了後の自動洗浄
動作の他に、−日の運転終了後に保守点検を行うように
しており、該保守点検として薬剤タンク3内に薬剤を投
薬して逆浸透式ろ過器lを洗浄するようにしている。In addition to the above-mentioned automatic cleaning operation after the completion of freshwater production, which is performed every time water production is completed, maintenance and inspection are performed after the completion of the production on -day, and as part of this maintenance and inspection, chemicals are dispensed into the chemical tank 3. I am trying to clean the reverse osmosis filter l.
上記各造水運転終了後の自動洗浄運転及び1日の運転終
了後に洗浄スイッチBをオンして行う洗浄運転は、いず
れも同様の動作で行なわれ、単に、運転スタートが自動
か、スイッチによるオン操作かの相違に過ぎない。よっ
て、洗浄スイッチBをオンした場合について説明すると
、洗浄スイッチBがオンされると、モータ27が駆動す
ると同時に、第2電磁弁6が動作して配管17と19を
連通させ、配管17と8の連通を遮断する。モータ・2
7の駆動により、前記の造水運転時と同様に、海水を逆
浸透式ろ過器lへ導入し、ろ過水を生成する。生成され
たろ過水は配管17、第2電磁弁6、配% 1gを通っ
て薬剤タンク3へ導入され、貯溜される。薬剤タンク3
内の貯溜液がほぼ満水となるとスイッチCがオンする。The automatic cleaning operation after each of the fresh water production operations described above and the cleaning operation performed by turning on the cleaning switch B after the end of one day's operation are all performed in the same way, and the operations are simply started automatically or turned on by a switch. It's just a difference in operation. Therefore, to explain the case where the cleaning switch B is turned on, when the cleaning switch B is turned on, the motor 27 is driven and at the same time, the second solenoid valve 6 is operated to connect the pipes 17 and 19, and the pipes 17 and 8 communication is cut off. Motor 2
7, seawater is introduced into the reverse osmosis filter 1 to produce filtrated water, as in the freshwater generation operation described above. The generated filtrate water is introduced into the chemical tank 3 through the pipe 17, the second electromagnetic valve 6, and the 1g portion, and is stored therein. Drug tank 3
When the reservoir liquid in the tank becomes almost full, switch C is turned on.
該スイッチCのオンにより連動して、第1電磁弁5が動
作され、配管10を洗浄液供給管夏2と連通し、かつ、
排水管23に介設した第4W1磁弁24を開き、プラン
ジャー・ポンプ4を低圧に設定する。When the switch C is turned on, the first solenoid valve 5 is operated to connect the pipe 10 with the cleaning liquid supply pipe 2, and
The fourth W1 magnetic valve 24 provided in the drain pipe 23 is opened, and the plunger pump 4 is set to low pressure.
よって、薬剤タンク3内の洗浄液は、洗浄液供給管12
、第1電磁弁5、配管IO、プランジャー・ポンプ4を
通して逆浸透式ろ過器1に供給され、半透膜100を含
むろ過器1の内部を洗浄する。ろ過器lを通った洗浄液
は大部分が第2出水口1cより排水管22、調圧弁26
、排水管21を通って排水され、一部分は半透膜100
を通って純水となり、第1出水口1bより配管17、第
27t!磁弁6、配管19を経て薬剤タンク3内に循環
される。Therefore, the cleaning liquid in the chemical tank 3 is transferred to the cleaning liquid supply pipe 12.
, the first electromagnetic valve 5, the piping IO, and the plunger pump 4 to be supplied to the reverse osmosis type filter 1 to clean the inside of the filter 1 including the semipermeable membrane 100. Most of the cleaning liquid that has passed through the filter l is transferred from the second water outlet 1c to the drain pipe 22 and the pressure regulating valve 26.
, the water is drained through the drain pipe 21, and a part of the water is drained through the semipermeable membrane 100.
The pure water flows through the first water outlet 1b to the pipe 17 and the 27th t! It is circulated into the drug tank 3 via the magnetic valve 6 and piping 19.
薬剤タンク3内の洗浄液がほぼ無くなると、マイコンM
が検知してモータ27が停止し、かつ、第1電磁弁5、
第2電磁弁6が動作されて初期位置に自動復帰され、洗
浄が自動的に停止する。When the cleaning liquid in the chemical tank 3 is almost exhausted, the microcomputer M
is detected and the motor 27 is stopped, and the first solenoid valve 5,
The second solenoid valve 6 is operated and automatically returned to the initial position, and the cleaning is automatically stopped.
尚、上記実施例は、海水を淡水化する場合に用いている
が、河川からの川水あるいは水道水を原水とする場合に
も当然のことながら用いることが出来る。Although the above embodiment is used for desalinating seawater, it can of course also be used when raw water is river water or tap water.
発明の効果
以上の説明より明らかなように、本発明に係わる装置に
よれば、オン・オフ操作される造水スイッチ(メインス
イッチ)と洗浄スイッチを池のスイッチおよび電磁弁と
連動させて本装置を自動制御する方式を採用しているた
め、造水および洗浄を誤動作なく簡単に行うことが出来
る。特に、この種の装置において必須の逆浸透式ろ過器
の洗浄が、各使用後毎に自動で行われ、該洗浄時に必要
な水圧の調整も、従来はその都度手動で行う必要があっ
たが、自動的に水圧が切り替えられる事などより、使用
毎の洗浄(保守、点検)が自動的に行える。よっ・て、
装置、特に、半透膜の耐久性を著しく向上させることが
出来、かつ、造水の生産性を飛躍的に向上させることが
でき、しかも、より安全性の高い飲料水が常に得られる
。Effects of the Invention As is clear from the above explanation, according to the device according to the present invention, the water production switch (main switch) and the cleaning switch, which are operated on and off, are linked with the pond switch and the solenoid valve. Since it uses an automatic control method, water production and cleaning can be easily performed without malfunction. In particular, the reverse osmosis filter, which is essential for this type of equipment, is automatically cleaned after each use, and the water pressure required for cleaning had to be adjusted manually each time in the past. By automatically switching the water pressure, cleaning (maintenance, inspection) can be performed automatically after each use. Yo, te,
The durability of the device, especially the semipermeable membrane, can be significantly improved, the productivity of water generation can be dramatically improved, and moreover, safer drinking water can always be obtained.
また、逆浸透式ろ過器によりろ過されただけの純水は、
無味乾燥で且つ自然に放置しておくと雑菌が繁殖しやす
い欠点を有しているが、本装置では、ろ過水を活性器に
通して、ミネラル化して飲料水に適した味とすると共に
、制菌作用を施して雑菌の繁殖を防いでおり、飲料水に
うま味と安全性を付与することが出来る。In addition, pure water that has just been filtered by a reverse osmosis filter is
It has the disadvantage of being tasteless and dry and prone to bacterial growth if left alone, but with this device, the filtered water is passed through an activator to mineralize it and give it a taste suitable for drinking water. It has antibacterial properties and prevents the growth of bacteria, making it possible to add flavor and safety to drinking water.
さらに、逆浸透式ろ過器を用いているため、蒸発型のよ
うに大量のエネルギーを必要とせず、コストを低下でき
る。しかも、装置自体が小型であり、据付時には、電気
回路を電源と接続し、飲料水のパイプと配管を接続する
だけであるため、どんな場所にも簡単に設置することが
出来る等の種々の利点を有するものである。Furthermore, since it uses a reverse osmosis type filter, it does not require a large amount of energy unlike the evaporation type, reducing costs. Moreover, the device itself is small, and during installation, all you have to do is connect the electric circuit to the power source and the drinking water pipes and piping, so it can be easily installed in any location. It has the following.
第1図は本装置の構成を示す全体概略図、第2図は逆浸
透式ろ過器の原理を示す図面、第3図は活性器の概略断
面図である。
l・・逆浸透式ろ過器、2・・活性器、3・・薬剤タン
ク、4・・プランジャ・ポンプ、5・・第1N磁弁、6
・・第2電磁弁、7・・第3電磁弁、24・・第3電磁
弁、27・・モータ、
A・・メインスイッチ、B・・洗浄スイッチ。FIG. 1 is an overall schematic diagram showing the configuration of the present device, FIG. 2 is a drawing showing the principle of a reverse osmosis filter, and FIG. 3 is a schematic sectional view of an activator. l... Reverse osmosis filter, 2... activator, 3... drug tank, 4... plunger pump, 5... 1st N magnetic valve, 6
...Second solenoid valve, 7..Third solenoid valve, 24..Third solenoid valve, 27..Motor, A..Main switch, B..Cleaning switch.
Claims (1)
る逆浸透式ろ過器と、ミネラル分を溶出する粒子および
滅菌作用を有する粒子等の複数種の粒子を筒体内に充填
して該筒体内部を通過するろ過水を活性化する活性器と
、薬剤タンクを備え、上記逆浸透式ろ過器の入水口をポ
ンプを介設した配管に接続し、該配管を流路切替用の第
1電磁弁を介して上記薬剤タンクに接続した洗浄液供給
管と海水取入管とに選択的に接続する一方、逆浸透式ろ
過器の出水口を流路切替用の第2電磁弁を介し上記活性
器と薬剤タンクに選択的に接続し、かつ、上記プランジ
ャ・ポンプをオン・オフ操作され造水スイッチと洗浄ス
イッチとにより始動・停止されるモータにより駆動させ
ると共に、上記スイッチに上記電磁弁等を連動させて造
水および洗浄作動を自動制御する構成とし、造水時には
、海水取入管から海水を逆浸透式ろ過器に供給し、該ろ
過器でろ過した水を活性器を通して飲料水配管へ導出す
る一方、洗浄時にはろ過水を薬剤タンクに導入して、設
定量に達すると上記洗浄液供給管より逆浸透式ろ過器へ
循環させる構成としていることを特徴とする海水淡水化
装置。1. A reverse osmosis filter that filters introduced seawater through a semipermeable membrane to pure water, and a cylinder filled with multiple types of particles, including particles that elute minerals and particles that have a sterilizing effect. The water inlet of the reverse osmosis filter is connected to piping with a pump interposed therein, and the piping is used for flow path switching. is selectively connected to the cleaning liquid supply pipe and the seawater intake pipe connected to the chemical tank through a first solenoid valve, while the water outlet of the reverse osmosis filter is connected through a second solenoid valve for flow path switching. The electromagnetic valve is selectively connected to the activator and the chemical tank, and the plunger pump is driven by a motor that is turned on and off and started and stopped by a water production switch and a cleaning switch, and the electromagnetic valve is connected to the switch. The system automatically controls water production and cleaning operations by linking the above, and when producing water, seawater is supplied from the seawater intake pipe to a reverse osmosis filter, and the water filtered by the filter is passed through the activator to the drinking water pipe. A seawater desalination apparatus characterized in that the filtered water is introduced into a chemical tank during cleaning, and when a set amount is reached, the water is circulated through the cleaning liquid supply pipe to a reverse osmosis type filter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1324495A JPH03181386A (en) | 1989-12-12 | 1989-12-12 | Seawater desalting equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1324495A JPH03181386A (en) | 1989-12-12 | 1989-12-12 | Seawater desalting equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03181386A true JPH03181386A (en) | 1991-08-07 |
Family
ID=18166444
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1324495A Pending JPH03181386A (en) | 1989-12-12 | 1989-12-12 | Seawater desalting equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03181386A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0580585U (en) * | 1991-12-03 | 1993-11-02 | 株式会社オニック | Desalination equipment |
| JPH06210283A (en) * | 1993-01-19 | 1994-08-02 | Kosumosu Enterp:Kk | Water purifier |
| EP1240938A1 (en) * | 2001-03-14 | 2002-09-18 | Ludwig Michelbach | Reverse osmosis plant |
| WO2010007696A1 (en) * | 2008-07-18 | 2010-01-21 | Ikuta Kazumasa | Water purifier |
-
1989
- 1989-12-12 JP JP1324495A patent/JPH03181386A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0580585U (en) * | 1991-12-03 | 1993-11-02 | 株式会社オニック | Desalination equipment |
| JPH06210283A (en) * | 1993-01-19 | 1994-08-02 | Kosumosu Enterp:Kk | Water purifier |
| EP1240938A1 (en) * | 2001-03-14 | 2002-09-18 | Ludwig Michelbach | Reverse osmosis plant |
| EP2008703A1 (en) * | 2001-03-14 | 2008-12-31 | Ludwig Michelbach | Reverse osmosis plant |
| WO2010007696A1 (en) * | 2008-07-18 | 2010-01-21 | Ikuta Kazumasa | Water purifier |
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