JP2001293471A - Purified water making device - Google Patents

Purified water making device

Info

Publication number
JP2001293471A
JP2001293471A JP2000113656A JP2000113656A JP2001293471A JP 2001293471 A JP2001293471 A JP 2001293471A JP 2000113656 A JP2000113656 A JP 2000113656A JP 2000113656 A JP2000113656 A JP 2000113656A JP 2001293471 A JP2001293471 A JP 2001293471A
Authority
JP
Japan
Prior art keywords
purified water
reverse osmosis
water
purified
pump
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
Application number
JP2000113656A
Other languages
Japanese (ja)
Inventor
Shigeyoshi Nagaoka
茂好 長岡
Koji Yamamoto
孝二 山元
Yoshitoshi Hokke
義寿 法花
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
MIKUNI KIKAI KK
Original Assignee
MIKUNI KIKAI KK
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 MIKUNI KIKAI KK filed Critical MIKUNI KIKAI KK
Priority to JP2000113656A priority Critical patent/JP2001293471A/en
Publication of JP2001293471A publication Critical patent/JP2001293471A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a purified water making device solving the problem of pyrogen. SOLUTION: This purified water making device makes purified water filtered and purified with a reverse osmosis module 1 provided with a reverse osmosis membrane. A front stage of a booster pump 15 for feeding water to the reverse osmosis module 1 is connected to a delivery pipe line 30 of the purified water purified with the reverse osmosis module 1 through a circulation path 33 provided with a back pressure valve 35, and as the booster pump 15, a pump is used of variable transfer quantity type changing the transfer quantity in accordance with pressure of the purified water in the delivery pipe line 30. This pump directly feeds the purified water without storing it in a feed tank, and the variation of the use quantity of the purified water is coped with by circulation of the purified water and also changing the transfer quantity of the booster pump 15.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は精製水製造装置、殊
に人工透析用の精製水の製造に好適に用いることができ
る精製水製造装置に関するものである。
The present invention relates to an apparatus for producing purified water, and more particularly to an apparatus for producing purified water which can be suitably used for producing purified water for artificial dialysis.

【0002】[0002]

【従来の技術】人工透析用の精製水を製造する装置とし
て、従来より図2に示すものがある。これは市井水(水
道水)である原水をプレフィルター11と活性炭フィル
ター12及び軟水装置13並びにチェックフィルター1
4に通した後、加圧ポンプ15で逆浸透膜を備えた逆浸
透モジュール1に送り、逆浸透モジュール1を出た精製
水を供給タンク2に溜めるとともに、該供給タンク2内
の精製水を供給ポンプ20によって人工透析用に供給す
るものであり、この時、精製水の使用量変動に応じて、
ポンプ20で送り出す精製水の一部を循環路24を介し
て供給タンク2に戻すようにしてある。図中25は供給
タンク2内に配した紫外線殺菌灯である。
2. Description of the Related Art FIG. 2 shows a conventional apparatus for producing purified water for artificial dialysis. This is a process in which raw water, which is city water (tap water), is passed through a prefilter 11, an activated carbon filter 12, a water softener 13, and a check filter 1.
4, the water is sent to the reverse osmosis module 1 equipped with the reverse osmosis membrane by the pressurizing pump 15, and the purified water exiting the reverse osmosis module 1 is stored in the supply tank 2 and the purified water in the supply tank 2 is removed. It is supplied for artificial dialysis by the supply pump 20. At this time, according to the fluctuation of the amount of purified water used,
A part of the purified water sent out by the pump 20 is returned to the supply tank 2 through the circulation path 24. In the figure, reference numeral 25 denotes an ultraviolet germicidal lamp arranged in the supply tank 2.

【0003】[0003]

【発明が解決しようとする課題】ここにおいて、供給タ
ンク2内の精製水は、脱塩素処理された水であって雑菌
が繁殖しやすい状態にある上に、一部は循環することも
あって滞留時間が長くなりやすく、このために上記殺菌
灯25によって雑菌は死滅させることができるとはい
え、細菌性パイロジェン(エンドトキシン)や非細菌性
パイロジェンが精製水中に混入しやすいものであり、そ
してこれらパイロジェンが人工透析用の精製水に混入し
た場合、透析患者に発熱などの症状を引き起こす。
Here, the purified water in the supply tank 2 is dechlorinated water which is in a state where various germs are easy to propagate, and a part of the purified water is circulated. Although the residence time is likely to be long and bacteria can be killed by the germicidal lamp 25, bacterial pyrogen (endotoxin) and non-bacterial pyrogen are liable to be mixed into purified water. When pyrogen is mixed into purified water for artificial dialysis, it causes symptoms such as fever in dialysis patients.

【0004】本発明はこのような点に鑑みなされたもの
であって、その目的とするところはパイロジェンの問題
を解消することができる精製水製造装置を提供するにあ
る。
[0004] The present invention has been made in view of such a point, and an object of the present invention is to provide a purified water producing apparatus which can solve the problem of pyrogen.

【0005】[0005]

【課題を解決するための手段】しかして本発明は、逆浸
透膜を備えた逆浸透モジュールにより濾過精製した精製
水を製造する精製水製造装置において、逆浸透モジュー
ルに水を送り込む加圧ポンプの前段と、逆浸透モジュー
ルにて精製した精製水の吐出用配管とを吐出用配管内の
圧力に応じて開閉する弁を備えた循環路で接続するとと
もに、上記加圧ポンプとして上記吐出用配管内の精製水
圧力に応じて給送量を変更する給送量可変型のものを用
いていることに特徴を有している。
SUMMARY OF THE INVENTION The present invention provides a purified water producing apparatus for producing purified water filtered and purified by a reverse osmosis module having a reverse osmosis membrane. The former stage and a discharge pipe for purified water purified by the reverse osmosis module are connected by a circulation path provided with a valve that opens and closes according to the pressure in the discharge pipe, and the pressurized pump is connected to the inside of the discharge pipe. It is characterized in that a feed rate variable type that changes the feed rate according to the purified water pressure is used.

【0006】供給タンクに貯留させることなく精製水を
直接送り出すようにしたものであり、精製水の使用量変
動については精製水を循環させることと加圧ポンプの給
送量の変更で応ずるようにしたものである。
[0006] Purified water is directly sent out without being stored in a supply tank, and fluctuations in the amount of purified water used can be accommodated by circulating the purified water and changing the feed amount of a pressurizing pump. It was done.

【0007】[0007]

【発明の実施の形態】以下本発明を人工透析用精製水の
製造装置で示した実施の形態の一例に基づいて詳述する
と、図1において、市井水(水道水)である原水は原水
ポンプ10によって加圧されて活性炭フィルター12と
軟水装置13及び保安フィルター16側へ送り出され、
これらを通過して給水用配管18に至った水は、加圧ポ
ンプ15によって逆浸透膜を備えた逆浸透モジュール1
に送られる。逆浸透モジュール1を出た精製水は、前記
従来例のものと異なり、供給タンクに溜められることな
く、吐出用配管30により紫外線殺菌機26とエンドト
キシンカット用のUF膜27とを経て人工透析用に供給
される。逆浸透モジュール1における濃縮排水は、排水
用配管31により上記加圧ポンプ15の駆動用のモータ
の冷却に使用された後、ドレン5へと排水される。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in detail below with reference to an example of an embodiment shown in an apparatus for producing purified water for artificial dialysis. In FIG. 1, raw water which is city water (tap water) is raw water. Pressurized by the pump 10 and sent out to the activated carbon filter 12, the water softener 13 and the security filter 16 side,
Water passing through these and reaching the water supply pipe 18 is subjected to a reverse osmosis module 1 having a reverse osmosis membrane by a pressure pump 15.
Sent to The purified water exiting the reverse osmosis module 1 is not stored in a supply tank, but is stored in a supply tank, passes through an ultraviolet sterilizer 26 and a UF membrane 27 for endotoxin cutting, and is used for artificial dialysis. Supplied to The concentrated wastewater in the reverse osmosis module 1 is used for cooling the drive motor of the pressurizing pump 15 by the drainage pipe 31, and then drained to the drain 5.

【0008】ここにおいて、上記吐出用配管30におけ
る紫外線殺菌機26の下流側と、加圧ポンプ15の上流
側となる給水用配管18とが精製水循環路33によって
接続されており、また、排水用配管31と給水用配管1
8とが濃縮水循環路34によって接続されており、一部
の濃縮水は加圧ポンプ15の前段に戻されるようになっ
ている。図中P1〜P6は圧力センサー、C1〜C2は
水質センサ、F1〜F2は流量センサー、T1は温度セ
ンサーである。
Here, the downstream side of the ultraviolet sterilizer 26 in the discharge pipe 30 and the water supply pipe 18 upstream of the pressurizing pump 15 are connected by a purified water circulation path 33, Piping 31 and water supply piping 1
8 is connected by a concentrated water circulation path 34, and a part of the concentrated water is returned to a stage preceding the pressure pump 15. In the figure, P1 to P6 are pressure sensors, C1 and C2 are water quality sensors, F1 and F2 are flow rate sensors, and T1 is a temperature sensor.

【0009】そして、精製水循環路33中には吐出用配
管30内の水圧が所定値以上になった時に開く背圧弁
(リリーフバルブ)35を設けてある。また、ここでは
上記加圧ポンプ15としてその給送能力が可変となって
いるものを用いるとともに、吐出用配管30内の精製水
圧力を検出する圧力センサーP6の出力値に応じて給送
能力を変更するように設定してある。
A back pressure valve (relief valve) 35 is provided in the purified water circulation passage 33 to open when the water pressure in the discharge pipe 30 becomes higher than a predetermined value. In addition, here, a pump whose pumping capacity is variable is used as the pressurizing pump 15 and the pumping capacity is adjusted according to an output value of a pressure sensor P6 that detects purified water pressure in the discharge pipe 30. It is set to change.

【0010】この精製水製造装置では、原水は前述のよ
うに活性炭フィルター12や軟水装置13を経て逆浸透
モジュール1に至り、逆浸透モジュール1の逆浸透膜1
0を通過した精製水は、吐出用配管30を通じて人工透
析用に直接供給されるものであり、パイロジェン混入の
原因となっていた供給タンクに溜められることなく人工
透析に利用されることから、透析患者のパイロジェンに
よる問題を解決することができる。
In this purified water production apparatus, raw water reaches the reverse osmosis module 1 through the activated carbon filter 12 and the soft water device 13 as described above, and the reverse osmosis membrane 1 of the reverse osmosis module 1
The purified water that has passed through 0 is supplied directly to the artificial dialysis through the discharge pipe 30 and is used for the artificial dialysis without being stored in the supply tank that caused the contamination of the pyrogen. The problem caused by the patient's pyrogen can be solved.

【0011】そして、従来において供給タンクが担って
いた精製水の使用量変動の吸収は、ここでは精製水循環
路33を通じた精製水の循環と、加圧ポンプ15の給送
能力の変更とによって行っている。使用量が減少して吐
出用配管30内の圧力が上昇すれば、背圧弁35が開い
て精製水循環路33を通じて余剰精製水を加圧ポンプ1
5の前段に戻すものであり、また加圧ポンプ15の給送
能力を落とす。使用量が増加すれば、この時には背圧弁
35が閉じて精製水の全量を人工透析用に供給するとと
もに加圧ポンプ15の給送能力を高める。なお、稼働中
は加圧ポンプ15は常時運転を行って、逆浸透モジュー
ル1に常に水を流す連続運転を行う。
Here, the absorption of the fluctuation in the amount of purified water used in the conventional supply tank is performed by circulating the purified water through the purified water circulation path 33 and changing the supply capacity of the pressurizing pump 15. ing. When the amount of use decreases and the pressure in the discharge pipe 30 increases, the back pressure valve 35 opens and excess purified water is supplied through the purified water circulation path 33 to the pressure pump 1.
5, and reduces the feeding capacity of the pressurizing pump 15. If the amount of use increases, at this time, the back pressure valve 35 closes to supply the entire amount of purified water for artificial dialysis and to increase the supply capacity of the pressurizing pump 15. During operation, the pressurizing pump 15 always operates, and performs a continuous operation of constantly flowing water through the reverse osmosis module 1.

【0012】加圧ポンプ15の給送能力の変更は、予め
設定した圧力と圧力センサーP6で検出した吐出用配管
30内の精製水圧力との差を検出して、この差に応じて
加圧ポンプ15のモータへの供給電源の電源周波数を変
更することで行うことができるとともに、この時の制御
には比例制御、比例・積分・微分制御などを用いること
ができるが、給送能力を機械的に変更することで対応し
てもよい。
The supply capacity of the pressurizing pump 15 is changed by detecting a difference between a preset pressure and a pressure of purified water in the discharge pipe 30 detected by the pressure sensor P6, and pressurizing according to the difference. It can be performed by changing the power supply frequency of the power supply to the motor of the pump 15, and the control at this time can use proportional control, proportional / integral / differential control, etc. This may be dealt with by changing it.

【0013】また、精製水循環路33と吐出用配管30
とを背圧弁35を介して連通させているが、背圧弁35
に代えて吐出用配管30内の圧力検出用の圧力センサー
P6の出力で開閉される電磁弁を用いてもよい。
The purified water circulation path 33 and the discharge pipe 30
Are communicated through the back pressure valve 35, but the back pressure valve 35
Instead, an electromagnetic valve that is opened and closed by the output of the pressure sensor P6 for detecting the pressure in the discharge pipe 30 may be used.

【0014】精製水圧力は0.2〜5kg/cm2、望
ましくは1〜3kg/cm2に設定するのが好ましい。
この圧力が低すぎると、次工程への精製水の十分な送液
が難しくなり、高すぎると加圧ポンプ15として大容量
のものが必要となるほか、発熱が大きくて精製水の温度
が上がったりエネルギー消費量が大きくなる等の問題が
発生する。
The pressure of the purified water is preferably set at 0.2 to 5 kg / cm 2 , more preferably at 1 to 3 kg / cm 2 .
If the pressure is too low, it is difficult to sufficiently supply purified water to the next step. If the pressure is too high, a large-capacity pump 15 is required, and the temperature of the purified water rises due to large heat generation. Problems such as an increase in energy consumption occur.

【0015】[0015]

【発明の効果】以上のように本発明においては、逆浸透
膜を備えた逆浸透モジュールにより濾過精製した精製水
を製造する精製水製造装置において、逆浸透モジュール
に水を送り込む加圧ポンプの前段と、逆浸透モジュール
にて精製した精製水の吐出用配管とを背圧弁を備えた循
環路で接続するとともに、上記加圧ポンプとして上記吐
出用配管内の精製水圧力に応じて給送量を変更する給送
量可変型のものを用いていることから、パイロジェンの
混入の原因となる供給タンクへの貯留を行うことなく精
製水を直接送り出すものであり、このためにパイロジェ
ンに起因する透析患者の問題を解決することができる。
そして、供給タンクの廃止に伴う精製水の使用量変動に
ついては、吐出用配管に背圧弁を介して連通する精製水
循環路による精製水の循環の加圧ポンプの給送量の変更
で対応することができるものである。
As described above, according to the present invention, in a purified water producing apparatus for producing purified water filtered and purified by a reverse osmosis module equipped with a reverse osmosis membrane, a pre-stage of a pressure pump for feeding water to the reverse osmosis module is provided. And a discharge pipe for purified water purified by the reverse osmosis module, connected by a circulation path having a back pressure valve, and a feed rate according to the purified water pressure in the discharge pipe as the pressurizing pump. Since the variable feed rate variable type is used, purified water is directly sent out without storing it in the supply tank, which causes the contamination of pyrogen. Problem can be solved.
The fluctuation in the amount of purified water used due to the abolition of the supply tank should be dealt with by changing the feed rate of the pressurized pump for circulation of purified water through the purified water circulation path communicating with the discharge pipe via the back pressure valve. Can be done.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の実施の形態の一例の配管図である。FIG. 1 is a piping diagram of an example of an embodiment of the present invention.

【図2】従来例の配管図である。FIG. 2 is a piping diagram of a conventional example.

【符号の説明】[Explanation of symbols]

1 逆浸透モジュール 15 加圧ポンプ 30 吐出用配管 33 循環路 35 背圧弁 DESCRIPTION OF SYMBOLS 1 Reverse osmosis module 15 Pressure pump 30 Discharge pipe 33 Circulation path 35 Back pressure valve

───────────────────────────────────────────────────── フロントページの続き (72)発明者 法花 義寿 大阪市淀川区新高3丁目7番9号 ミクニ キカイ株式会社内 Fターム(参考) 4C077 AA05 BB01 DD14 KK11 NN20 4D006 GA05 GA06 JA53A JA56A JA57A JA58A JA65A KA02 KA03 KA16 KA52 KA55 KA57 KA63 KA71 KB04 KB11 KB12 KB14 KD19 KE03Q KE04P KE07P KE08R KE12P KE13P KE16P KE22Q KE23Q PA01 PB06 PB54 PC44  ────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Yoshihisa Hohana 3-7-9 Shindaka, Yodogawa-ku, Osaka Mikuni Kikai Corporation F-term (reference) 4C077 AA05 BB01 DD14 KK11 NN20 4D006 GA05 GA05 GA06 JA53A JA56A JA57A JA58A JA65A KA02 KA03 KA16 KA52 KA55 KA57 KA63 KA71 KB04 KB11 KB12 KB14 KD19 KE03Q KE04P KE07P KE08R KE12P KE13P KE16P KE22Q KE23Q PA01 PB06 PB54 PC44

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 逆浸透膜を備えた逆浸透モジュールによ
り濾過精製した精製水を製造する精製水製造装置におい
て、逆浸透モジュールに水を送り込む加圧ポンプの前段
と、逆浸透モジュールにて精製した精製水の吐出用配管
とを吐出用配管内の圧力に応じて開閉する弁を備えた循
環路で接続するとともに、上記加圧ポンプとして上記吐
出用配管内の精製水圧力に応じて給送量を変更する給送
量可変型のものを用いていることを特徴とする精製水製
造装置。
In a purified water producing apparatus for producing purified water filtered and purified by a reverse osmosis module having a reverse osmosis membrane, the purified water is purified by a pre-stage of a pressure pump for feeding water to the reverse osmosis module and a reverse osmosis module. The purified water discharge pipe is connected to a circulation path having a valve that opens and closes according to the pressure in the discharge pipe, and the feed rate according to the purified water pressure in the discharge pipe as the pressure pump. A purified water production apparatus characterized by using a variable feed rate type for changing the amount of water.
JP2000113656A 2000-04-14 2000-04-14 Purified water making device Pending JP2001293471A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000113656A JP2001293471A (en) 2000-04-14 2000-04-14 Purified water making device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000113656A JP2001293471A (en) 2000-04-14 2000-04-14 Purified water making device

Publications (1)

Publication Number Publication Date
JP2001293471A true JP2001293471A (en) 2001-10-23

Family

ID=18625583

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000113656A Pending JP2001293471A (en) 2000-04-14 2000-04-14 Purified water making device

Country Status (1)

Country Link
JP (1) JP2001293471A (en)

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JP2007152239A (en) * 2005-12-06 2007-06-21 Miura Co Ltd Membrane filtration system
JP2010253364A (en) * 2009-04-23 2010-11-11 Disco Abrasive Syst Ltd Pure water generator
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JP2014124482A (en) * 2012-12-27 2014-07-07 Nomura Micro Sci Co Ltd Method of sterilizing pure water production apparatus for pharmaceuticals and pure water production apparatus for pharmaceuticals
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JP2002126733A (en) * 2000-10-26 2002-05-08 Teraoka Seiko Co Ltd Water cleaning apparatus
JP2007029939A (en) * 2005-06-22 2007-02-08 Daicen Membrane Systems Ltd Apparatus for producing dialysis water and its sterilization method
JP2007152239A (en) * 2005-12-06 2007-06-21 Miura Co Ltd Membrane filtration system
JP2010253364A (en) * 2009-04-23 2010-11-11 Disco Abrasive Syst Ltd Pure water generator
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