JP2012200340A - Manufacturing device of dialysis solution preparation water - Google Patents

Manufacturing device of dialysis solution preparation water Download PDF

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JP2012200340A
JP2012200340A JP2011066064A JP2011066064A JP2012200340A JP 2012200340 A JP2012200340 A JP 2012200340A JP 2011066064 A JP2011066064 A JP 2011066064A JP 2011066064 A JP2011066064 A JP 2011066064A JP 2012200340 A JP2012200340 A JP 2012200340A
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reverse osmosis
osmosis membrane
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JP5153905B2 (en
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Nobukatsu Morisawa
紳勝 森澤
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Nihon Trim Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a manufacturing device of dialysis solution preparation water, capable of effectively washing a flow path of the entire device without damaging a reverse osmosis membrane treatment device.SOLUTION: The manufacturing device of dialysis solution preparation water includes an electrolytic water generator and the reverse osmosis membrane treatment device, executes reverse osmosis membrane treatment in the reverse osmosis membrane treatment device to electrolytic reduction water generated in the electrolytic water generator and supplies it for preparation of a dialysis solution. The manufacturing device of the dialysis solution preparation water includes a bypass flow path for connecting the upstream and downstream of the reverse osmosis membrane treatment device without interposing the reverse osmosis membrane treatment device.

Description

本発明は、透析液を調製するための透析液調製用水を製造するための装置に関する。   The present invention relates to an apparatus for producing dialysate preparation water for preparing a dialysate.

腎機能が低下し、水分量の調節と尿素などの老廃物を含む体内有害物質の除去を行うための尿の排泄ができない腎不全患者のための有効な治療法の一つに、血液透析が知られている。血液透析は、血液ポンプを用いて血液を体外に引き出し、これを透析器(ダイアライザー)を介して透析液と血液とを接触させることにより、濃度勾配による拡散現象を利用して体内有害物質および水分を除去した後、再び体内に戻す(返血)操作を連続して行う治療法である。   Hemodialysis is one of the effective treatments for renal failure patients who have impaired kidney function and cannot excrete urine to regulate water content and remove harmful substances such as urea. Are known. In hemodialysis, blood is drawn out of the body using a blood pump, and the dialysate and blood are brought into contact with each other through a dialyzer, so that harmful substances and water in the body are utilized by utilizing a diffusion phenomenon due to a concentration gradient. This is a treatment method in which the operation of returning the blood to the body (returning blood) is continuously performed after removing the blood.

図6は、従来の典型的な透析液用水処理システム101を示すブロック図である。たとえば、図6に示すように、従来の透析液用水処理システム101は、逆浸透膜処理装置102と、透析液供給装置103とを備える。逆浸透膜処理装置102では、原水(市水)104を加圧ポンプ105にて加圧し、10〜30μmの孔径のフィルター106にて原水104中の固形物を処理後、軟水器107で原水104の硬度を下げた後、活性炭108にて原水104に含まれる次亜塩素酸を除去する。その後、加圧ポンプ109で加圧した後、逆浸透膜110内を通水し、逆浸透膜を通過した精製水をROタンク111に貯水する。ROタンク111より精製水を加圧ポンプ112にて送水し、逆浸透膜処理装置102外へ送水配管113を通して送水し、透析液供給装置103に供給する。透析液供給装置103では、供給された精製水と透析A原液114および透析B原液115を混合し透析液として各患者監視装置(図示せず)へ供給され、患者監視装置に取り付けられているダイヤライザーを通して患者の血液の浄化が行われる。   FIG. 6 is a block diagram showing a conventional typical dialysate water treatment system 101. For example, as shown in FIG. 6, a conventional dialysate water treatment system 101 includes a reverse osmosis membrane treatment device 102 and a dialysate supply device 103. In the reverse osmosis membrane treatment apparatus 102, raw water (city water) 104 is pressurized with a pressure pump 105, solids in the raw water 104 are treated with a filter 106 having a pore size of 10 to 30 μm, and then the raw water 104 is treated with a water softener 107. Then, hypochlorous acid contained in the raw water 104 is removed by the activated carbon 108. Then, after pressurizing with the pressurizing pump 109, water is passed through the reverse osmosis membrane 110, and the purified water that has passed through the reverse osmosis membrane is stored in the RO tank 111. Purified water is supplied from the RO tank 111 by the pressure pump 112, supplied to the outside of the reverse osmosis membrane treatment device 102 through the water supply pipe 113, and supplied to the dialysate supply device 103. In the dialysate supply device 103, the supplied purified water, the dialysate A stock solution 114, and the dialysate B stock solution 115 are mixed and supplied as dialysate to each patient monitoring device (not shown) and attached to the patient monitoring device. The patient's blood is purified through the riser.

このような従来の透析液用水処理システム101における水の流路は、経時的にエンドトキシンが増加したり、患者監視装置やダイアライザーなどの血液環流配管に血液中のタンパク質が付着するという虞があるため、定期的に洗浄する必要がある。流路の洗浄方法としては、電気分解により生成された酸性水に含まれる次亜塩素酸を利用した殺菌洗浄方法が知られている。しかしながら、この方法は逆浸透膜処理装置102内の逆浸透膜が強アルカリ・強酸性への耐性が低いため、透析用水処理ラインの逆浸透膜処理装置以降の流路に酸性水を供給する必要があった。   In such a conventional water treatment system 101 for dialysate, the endotoxin may increase over time, or proteins in blood may adhere to blood circulation piping such as a patient monitoring device or a dialyzer. Need to be cleaned regularly. As a flow path cleaning method, a sterilization cleaning method using hypochlorous acid contained in acidic water generated by electrolysis is known. However, in this method, since the reverse osmosis membrane in the reverse osmosis membrane treatment apparatus 102 has low resistance to strong alkali and strong acid, it is necessary to supply acidic water to the flow path after the reverse osmosis membrane treatment apparatus in the dialysis water treatment line. was there.

ところで、近年、血液透析において透析患者に酸化ストレスが発生することが知られている。これは、透析時に発生する活性酸素が原因であると考えられており、この活性酸素を消去して酸化ストレスの軽減を図るための透析装置として、たとえば特許第3193295号(特許文献1)では、電気分解装置の電解槽内で陰極側に生成される電解還元水の持つ抗酸化作用を応用した透析装置が提案されている。   Incidentally, in recent years, it is known that oxidative stress occurs in dialysis patients in hemodialysis. This is considered to be caused by active oxygen generated during dialysis. For example, in Patent No. 3193295 (Patent Document 1) as a dialysis apparatus for eliminating this active oxygen and reducing oxidative stress, There has been proposed a dialysis apparatus that applies the antioxidant action of electroreduced water produced on the cathode side in an electrolytic cell of an electrolysis apparatus.

特許第3193295号Japanese Patent No. 3193295

本発明は上記課題を解決するためになされたものであって、その目的とするところは、逆浸透膜処理装置にダメージを与えることなく、装置全体の流路を効果的に洗浄することができる透析液調製用水の製造装置を提供することである。   The present invention has been made to solve the above-mentioned problems, and the object of the present invention is to effectively clean the flow path of the entire apparatus without damaging the reverse osmosis membrane treatment apparatus. It is to provide a device for producing dialysate preparation water.

本発明は、電解水生成装置と逆浸透膜処理装置とを備え、電解水生成装置で生成された電解還元水を逆浸透膜処理装置で逆浸透膜処理して透析液の調製に供する透析液調製用水の製造装置であって、逆浸透膜処理装置の上流および下流を当該逆浸透膜処理装置を介さずに連結するバイパス流路を備える透析液調製用水の製造装置である。   The present invention comprises an electrolyzed water generating device and a reverse osmosis membrane treatment device, and a dialysate for preparing a dialysate by subjecting electrolytic reduced water produced by the electrolyzed water production device to reverse osmosis membrane treatment with a reverse osmosis membrane treatment device An apparatus for producing preparation water, the apparatus for producing dialysate preparation water comprising a bypass channel that connects upstream and downstream of a reverse osmosis membrane treatment apparatus without using the reverse osmosis membrane treatment apparatus.

本発明の透析液調製用水の製造装置は、流路に電解水生成装置で生成した水を通過させて、流路を洗浄する機能を備えることが好ましい。   It is preferable that the apparatus for producing dialysate preparation water of the present invention has a function of allowing the water generated by the electrolyzed water generating device to pass through the channel and washing the channel.

本発明の透析液調製用水の製造装置は、電解水生成装置で生成した水を逆浸透処理装置を通過させずにバイパス流路を通過させることが好ましい。この場合、電解水生成装置で生成した水のpHは11以上またはpH3以下であることが好ましい。   The apparatus for producing dialysate preparation water according to the present invention preferably allows the water generated by the electrolyzed water generator to pass through the bypass channel without passing through the reverse osmosis treatment device. In this case, the pH of the water generated by the electrolyzed water generator is preferably 11 or more or pH 3 or less.

また、本発明の透析液調製用水の製造装置は、電解水生成装置で生成した水を逆浸透処理装置を通過させるようにしてもよい。この場合、電解水生成装置で生成した水のpHは3を超えて6.5以下であることが好ましい。   Moreover, you may make it the water manufacturing apparatus of the dialysate preparation water of this invention pass the water produced | generated with the electrolyzed water production | generation apparatus through a reverse osmosis processing apparatus. In this case, it is preferable that pH of the water produced | generated with the electrolyzed water production | generation apparatus exceeds 3 and is 6.5 or less.

本発明の透析液調製用水の製造装置によれば、逆浸透膜処理装置にダメージを与えることなく、装置全体の流路を効果的に洗浄することができる。   According to the apparatus for producing dialysate preparation water of the present invention, the flow path of the entire apparatus can be effectively washed without damaging the reverse osmosis membrane treatment apparatus.

本発明の好ましい一例の透析液調製用水の製造装置1を示すブロック図である。It is a block diagram which shows the manufacturing apparatus 1 of the water for dialysate preparation of a preferable example of this invention. 本発明の透析液調製用水の製造装置1における電解水生成装置2および流路切替装置9を拡大して示す図である。It is a figure which expands and shows the electrolyzed water production | generation apparatus 2 and the flow-path switching apparatus 9 in the manufacturing apparatus 1 of the dialysate preparation water of this invention. 電解強還元水を用いて流路を洗浄する場合の電解水生成装置2および流路切替装置9を拡大して示す図である。It is a figure which expands and shows the electrolyzed water production | generation apparatus 2 and the flow-path switching apparatus 9 in the case of wash | cleaning a flow path using electrolyzed strong reduced water. 電解強酸性水を用いて流路を洗浄する場合の電解水生成装置2および流路切替装置9を拡大して示す図である。It is a figure which expands and shows the electrolyzed water production | generation apparatus 2 and the flow-path switching apparatus 9 in the case of wash | cleaning a flow path using electrolysis strong acid water. 電解酸性水を用いて流路を洗浄する場合の電解水生成装置2および流路切替装置9を拡大して示す図である。It is a figure which expands and shows the electrolyzed water production | generation apparatus 2 and the flow-path switching apparatus 9 in the case of wash | cleaning a flow path using electrolytic acid water. 従来の典型的な透析液用水処理システム101を示すブロック図である。It is a block diagram which shows the conventional typical dialysate water treatment system.

図1は、本発明の好ましい一例の透析液調製用水の製造装置1を示すブロック図である。本発明の透析液調製用水の製造装置1は、電解水生成装置2と逆浸透膜処理装置3とを備え、電解水生成装置2で生成された電解還元水を逆浸透膜処理装置3で逆浸透膜処理することで、抗酸化作用を持った電解還元水を透析液原液の希釈液(透析液調製用水)として供給する。   FIG. 1 is a block diagram showing a manufacturing apparatus 1 for dialysate preparation water, which is a preferred example of the present invention. An apparatus for producing dialysate preparation water 1 according to the present invention includes an electrolyzed water generating device 2 and a reverse osmosis membrane treatment device 3, and the electrolytic reduced water produced by the electrolyzed water production device 2 is reversed by the reverse osmosis membrane treatment device 3. By carrying out the osmosis membrane treatment, electrolytically reduced water having an antioxidant action is supplied as a diluting solution of the dialysate stock solution (dialysate preparation water).

図1に示す例の透析液調製用水の製造装置1は、上述した電解水生成装置2およびバイパス流路(後述)を備えること以外は、図6に示した従来の透析液用水処理システム101の逆浸透膜処理装置102と同様の構成を備える。具体的には、図1に示す例の透析液調製用水の製造装置1は、原水(市水)4を加圧ポンプ5にて加圧し、10〜30μmの孔径のフィルター6にて原水4中の固形物を処理後、軟水器7で原水4の硬度を下げた後、活性炭8にて原水4に含まれる次亜塩素酸を除去するように構成される。活性炭8を通過した水は、電解水生成装置2に供され、電気分解される。本発明の透析液調製用水の製造装置1では、電解水生成装置2は、流路切替装置9に連結され、電解水生成装置2で得られた水を用途に応じて流す経路を切り替えることができるように構成されている。   The dialysate preparation water manufacturing apparatus 1 of the example shown in FIG. 1 is the same as the conventional dialysate water treatment system 101 shown in FIG. 6 except that it includes the above-described electrolyzed water generation apparatus 2 and a bypass channel (described later). A configuration similar to that of the reverse osmosis membrane treatment apparatus 102 is provided. Specifically, the apparatus 1 for preparing dialysis fluid preparation water in the example shown in FIG. 1 pressurizes raw water (city water) 4 with a pressure pump 5, and in the raw water 4 with a filter 6 having a pore diameter of 10 to 30 μm. After the solid matter is treated, the hardness of the raw water 4 is lowered by the water softener 7 and then the hypochlorous acid contained in the raw water 4 is removed by the activated carbon 8. The water that has passed through the activated carbon 8 is supplied to the electrolyzed water generator 2 and electrolyzed. In the dialysate preparation water production apparatus 1 of the present invention, the electrolyzed water generating device 2 is connected to the flow path switching device 9 and can switch the flow path of the water obtained by the electrolyzed water generating device 2 depending on the application. It is configured to be able to.

ここで、図2は、本発明の透析液調製用水の製造装置1における電解水生成装置2および流路切替装置9を拡大して示す図である。本発明の透析液調製用水の製造装置に用いられる電解水生成装置は、当分野において通常用いられる電解水生成装置であればよく、特に制限されるものではない。図2に示す例の電解水生成装置2は、隔膜11で同じ容積を有する2つの電解室13,14に分離された電解槽12を備える。電極室13,14には、それぞれ電極15,16が設置されている。   Here, FIG. 2 is an enlarged view of the electrolyzed water generating device 2 and the flow path switching device 9 in the dialysate preparation water producing apparatus 1 of the present invention. The electrolyzed water generator used in the apparatus for producing dialysate preparation water of the present invention is not particularly limited as long as it is an electrolyzed water generator normally used in this field. The electrolyzed water generating apparatus 2 of the example shown in FIG. 2 includes an electrolytic cell 12 separated into two electrolysis chambers 13 and 14 having the same volume by a diaphragm 11. Electrodes 15 and 16 are installed in the electrode chambers 13 and 14, respectively.

図2に示す電解水生成装置2において、電解室13に流入する原水は水量調整バルブ17にて調整可能であるように構成される。当該電解水生成装置2で生成した電解還元水を透析液調製用水として供する場合、水量調整バルブ17によって、電解室13に流入させる原水を、電解室14に流入する水量より少なく設定する(たとえば、電解室14に流入する量の1/5)。そうすることにより、電解室13に流入する量は少なくなり、しかも電解室13の容積は電解室14と同じ容積で設計されているため、電解室13内での原水の流速は電解室14内の流速より遅く(1/5)なり、原水が電解室13内を通過する時間は原水が電解室14内を通過する時間より長くなることとなる。これにより、電極板15を陽極、電極板16を陰極として電気分解すると、電解室13では電気分解される時間が長くなることとなり、強く電気分解されることになる。このようにすることで、電解室13ではpH3以下の電解酸性水(電解強酸性水)が生成され、電解室14では電解還元水が生成されることとなる。   In the electrolyzed water generating apparatus 2 shown in FIG. 2, the raw water flowing into the electrolysis chamber 13 is configured to be adjustable by a water amount adjusting valve 17. When the electrolytically reduced water generated by the electrolyzed water generating device 2 is used as dialysate preparation water, the water amount adjusting valve 17 sets the raw water flowing into the electrolysis chamber 13 to be smaller than the amount of water flowing into the electrolysis chamber 14 (for example, 1/5 of the amount flowing into the electrolysis chamber 14). By doing so, the amount flowing into the electrolysis chamber 13 is reduced, and the volume of the electrolysis chamber 13 is designed to be the same as that of the electrolysis chamber 14, so the flow rate of raw water in the electrolysis chamber 13 is within the electrolysis chamber 14. Therefore, the time for the raw water to pass through the electrolysis chamber 13 is longer than the time for the raw water to pass through the electrolysis chamber 14. As a result, when electrolysis is performed using the electrode plate 15 as an anode and the electrode plate 16 as a cathode, the electrolysis time in the electrolysis chamber 13 becomes longer and the electrolysis is strongly electrolyzed. By doing so, electrolytic acid water having a pH of 3 or less (electrolytic strongly acidic water) is generated in the electrolysis chamber 13, and electrolytic reduction water is generated in the electrolysis chamber 14.

当該電解水生成装置2で生成した電解還元水を透析液調製用水として供する場合、流路切替装置9内の切替バルブ18により、電解室13で生成された電解強酸性水を排水し、かつ、切替バルブ19により、電解室14で生成された電解還元水は電解水タンク20に給水される。電解水タンク20に供給された電解還元水は、加圧ポンプ21で加圧され、逆浸透膜処理装置3内で逆浸透膜を通過する。逆浸透膜を通過した後の電解還元水は、ROタンク22に貯水される。ROタンク22に貯められた電解還元水は、加圧ポンプ23にて加圧され、透析液調製用水の製造装置1の外に送水配管24を通して送水し、図6に示したような透析液供給装置103に供給される。   When electrolytically reduced water generated by the electrolyzed water generating device 2 is used as dialysate preparation water, the electrolyzed acidic water generated in the electrolysis chamber 13 is drained by the switching valve 18 in the flow path switching device 9, and The electrolytically reduced water produced in the electrolysis chamber 14 is supplied to the electrolyzed water tank 20 by the switching valve 19. The electrolytically reduced water supplied to the electrolyzed water tank 20 is pressurized by the pressurizing pump 21 and passes through the reverse osmosis membrane in the reverse osmosis membrane treatment apparatus 3. The electrolytically reduced water after passing through the reverse osmosis membrane is stored in the RO tank 22. The electrolytically reduced water stored in the RO tank 22 is pressurized by the pressurizing pump 23 and is supplied to the outside of the dialysate preparation water production apparatus 1 through the water supply pipe 24 to supply the dialysate as shown in FIG. Supplied to the device 103.

本発明の透析液調製用水の製造装置1は、流路に電解水生成装置で生成した水を通過させて、流路を洗浄する機能を備えることが好ましい。なお、電解水生成装置で生成した水は、そのpHによって、たとえば電解還元水(pHが8以上11以下)、電解強還元水(pHが11を超える)、電解酸性水(pHが3を超えて6.5以下)、電解強酸性水(pHが3以下)に分類して呼称する。   The dialysis solution preparation water production apparatus 1 of the present invention preferably has a function of allowing water generated by the electrolyzed water generating device to pass through the flow path and washing the flow path. In addition, the water produced | generated with the electrolyzed water production | generation apparatus depends on the pH, for example, electrolytic reduction water (pH is 8 or more and 11 or less), electrolytic strong reduction water (pH exceeds 11), electrolytic acid water (pH exceeds 3). 6.5 or less) and electrolytically strongly acidic water (pH is 3 or less).

ここで、本発明の透析液調製用水の製造装置1は、逆浸透膜処理装置3の上流および下流を当該逆浸透膜処理装置3を介さずに連結するバイパス流路31を備えることを大きな特徴とする。本発明の透析液調製用水の製造装置1は、電解水生成装置で生成した水を逆浸透処理装置を通過させずにバイパス流路を通過させることで、流路の洗浄を行うことが好ましい。   Here, the manufacturing apparatus 1 for dialysate preparation water according to the present invention includes a bypass channel 31 that connects the upstream and downstream of the reverse osmosis membrane treatment device 3 without using the reverse osmosis membrane treatment device 3. And The dialysis fluid preparation water producing apparatus 1 of the present invention preferably cleans the flow path by allowing the water generated by the electrolyzed water generating apparatus to pass through the bypass flow path without passing through the reverse osmosis treatment apparatus.

図3は、電解強還元水を用いて流路を洗浄する場合の電解水生成装置2および流路切替装置9を拡大して示す図である。電解水生成装置2内の電解槽12の電極板15を陰極、電極板16を陽極として電気分解することで、電解室13には電解強還元水が生成され、電解室14には電解酸性水が生成される。切替バルブ18により電解室13で生成した電解強還元水は電解水タンク20に給水され、電解水タンク20に貯水された後、洗浄に利用される。pH11を超える電解還元水である電解強還元水は、流路に付着した血液に含まれるタンパク質の洗浄に有用である。しかしながら、電解強還元水は逆浸透膜にダメージを与えるため、電解強還元水を用いた洗浄を行う場合には、バイパス用切替バルブ32,33によって、電解強還元水が逆浸透膜処理装置3を通過せずバイパス経路31を通過するようにする。このような本発明の透析液調製用水の製造装置によれば、逆浸透膜処理装置にダメージを与えることなく、装置全体の流路を効果的に洗浄することができる。一方、流路切替装置9において、電解室14で生成された電解酸性水は、切替バルブ19によって排水される。   FIG. 3 is an enlarged view showing the electrolyzed water generating device 2 and the flow path switching device 9 when the flow path is cleaned using electrolytically strong reduced water. Electrolyzed with the electrode plate 15 of the electrolytic cell 12 in the electrolyzed water generating device 2 as a cathode and the electrode plate 16 as an anode, electrolyzed strong reduced water is produced in the electrolysis chamber 13, and electrolyzed acidic water is produced in the electrolysis chamber 14. Is generated. The electrolytically strong reduced water generated in the electrolysis chamber 13 by the switching valve 18 is supplied to the electrolyzed water tank 20 and stored in the electrolyzed water tank 20 and then used for cleaning. Electrolytically reduced water, which is electrolytically reduced water exceeding pH 11, is useful for washing proteins contained in blood adhering to the flow path. However, since the strong electrolytically reduced water damages the reverse osmosis membrane, when the electrolytic strong reduced water is washed, the electrolytically strong reduced water is converted into the reverse osmosis membrane treatment device 3 by the bypass switching valves 32 and 33. Pass the bypass path 31 without passing through. According to such a dialysis fluid preparation water production apparatus of the present invention, the flow path of the entire apparatus can be effectively washed without damaging the reverse osmosis membrane treatment apparatus. On the other hand, in the flow path switching device 9, the electrolytic acid water generated in the electrolysis chamber 14 is drained by the switching valve 19.

また図4は、電解強酸性水を用いて流路を洗浄する場合の電解水生成装置2および流路切替装置9を拡大して示す図である。電解水生成装置2内の電解槽12の電極板15を陽極、電極板16を陰極として電気分解することで、電解室13には電解強酸性水が生成され、電解室14には電解還元水が生成される。切替バルブ18により電解室13で生成した電解強酸性水は電解水タンク20に給水され、電解水タンク20に貯水された後、洗浄に利用される。pHが3.0以下である電解強酸性水は、逆浸透膜にダメージを与えるため、電解強酸性水を用いた洗浄を行う場合には、バイパス用切替バルブ32,33によって、電解強酸性水が逆浸透膜処理装置3を通過せずバイパス経路31を通過するようにする。このような本発明の透析液調製用水の製造装置によれば、逆浸透膜処理装置にダメージを与えることなく、装置全体の流路を効果的に洗浄することができる。一方、流路切替装置9において、電解室14で生成された電解還元水は、切替バルブ19によって排水される。   FIG. 4 is an enlarged view showing the electrolyzed water generating device 2 and the flow channel switching device 9 when the flow channel is washed using electrolytically strong acidic water. Electrolysis is performed using the electrode plate 15 of the electrolytic cell 12 in the electrolyzed water generator 2 as an anode and the electrode plate 16 as a cathode, whereby electrolytically acidic water is generated in the electrolysis chamber 13 and electroreduction water is generated in the electrolysis chamber 14. Is generated. The electrolyzed acidic water generated in the electrolysis chamber 13 by the switching valve 18 is supplied to the electrolyzed water tank 20, stored in the electrolyzed water tank 20, and then used for cleaning. Electrolytically strong acidic water having a pH of 3.0 or less damages the reverse osmosis membrane. Therefore, when washing with electrolytically strong acidic water is performed, electrolytic strong acidic water is bypassed by the bypass switching valves 32 and 33. Pass through the bypass path 31 without passing through the reverse osmosis membrane treatment apparatus 3. According to such a dialysis fluid preparation water production apparatus of the present invention, the flow path of the entire apparatus can be effectively washed without damaging the reverse osmosis membrane treatment apparatus. On the other hand, in the flow path switching device 9, the electrolytic reduced water generated in the electrolysis chamber 14 is drained by the switching valve 19.

また図5は、電解酸性水を用いて流路を洗浄する場合の電解水生成装置2および流路切替装置9を拡大して示す図である。上述のように、電解水生成装置2内の電解槽12の電極板15を陰極、電極板16を陽極として電気分解することで、電解室13には電解強還元水が生成され、電解室14には電解酸性水が生成される。切替バルブ19により電解室14で生成した電解酸性水は電解水タンク20に給水され、電解水タンク20に貯水された後、洗浄に利用される。pHが3.0を超えて6.5以下である電解酸性水は、逆浸透膜にダメージを与えないので、逆浸透膜処理装置内にも流して洗浄することができる。一方、流路切替装置9において、電解室13で生成された電解強還元水は、切替バルブ18によって排水される。   FIG. 5 is an enlarged view showing the electrolyzed water generating device 2 and the flow path switching device 9 when the flow path is cleaned using electrolytic acid water. As described above, electrolyzed electrolytically reduced water is generated in the electrolysis chamber 13 by electrolysis using the electrode plate 15 of the electrolytic cell 12 in the electrolyzed water generating apparatus 2 as a cathode and the electrode plate 16 as an anode. Electrolytic acid water is generated in The electrolyzed acidic water generated in the electrolysis chamber 14 by the switching valve 19 is supplied to the electrolyzed water tank 20 and stored in the electrolyzed water tank 20 and then used for cleaning. Electrolytic acid water having a pH of more than 3.0 and not more than 6.5 does not damage the reverse osmosis membrane, so that it can be washed by flowing it into the reverse osmosis membrane treatment apparatus. On the other hand, in the flow path switching device 9, the electrolytically strong reduced water generated in the electrolysis chamber 13 is drained by the switching valve 18.

Claims (7)

電解水生成装置と逆浸透膜処理装置とを備え、電解水生成装置で生成された電解還元水を逆浸透膜処理装置で逆浸透膜処理して透析液の調製に供する透析液調製用水の製造装置であって、
逆浸透膜処理装置の上流および下流を当該逆浸透膜処理装置を介さずに連結するバイパス流路を備える、透析液調製用水の製造装置。
Manufacture of water for dialysate preparation, which comprises an electrolyzed water generator and a reverse osmosis membrane treatment device, and uses electrolytic reduced water produced by the electrolyzed water generator for reverse osmosis membrane treatment for the preparation of dialysate A device,
An apparatus for producing dialysate preparation water, comprising a bypass channel that connects upstream and downstream of a reverse osmosis membrane treatment apparatus without using the reverse osmosis membrane treatment apparatus.
流路に電解水生成装置で生成した水を通過させて、流路を洗浄する機能を備える、請求項1に記載の装置。   The apparatus of Claim 1 provided with the function which makes the flow path pass the water produced | generated with the electrolyzed water generating apparatus, and wash | cleans a flow path. 電解水生成装置で生成した水を逆浸透処理装置を通過させずにバイパス流路を通過させる、請求項2に記載の装置。   The apparatus according to claim 2, wherein water generated by the electrolyzed water generating apparatus is allowed to pass through the bypass flow path without passing through the reverse osmosis treatment apparatus. 電解水生成装置で生成した水のpHが11以上である、請求項3に記載の装置。   The apparatus of Claim 3 whose pH of the water produced | generated with the electrolyzed water production | generation apparatus is 11 or more. 電解水生成装置で生成した水のpH3以下である、請求項3に記載の装置。   The apparatus of Claim 3 which is pH 3 or less of the water produced | generated with the electrolyzed water production | generation apparatus. 電解水生成装置で生成した水を逆浸透処理装置を通過させる、請求項2に記載の装置。   The apparatus of Claim 2 which passes the water produced | generated with the electrolyzed water production | generation apparatus through the reverse osmosis processing apparatus. 電解水生成装置で生成した水のpHが3を超えて6.5以下である、請求項6に記載の装置。   The apparatus of Claim 6 whose pH of the water produced | generated with the electrolyzed water production | generation apparatus exceeds 3 and is 6.5 or less.
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