JP3473866B2 - Membrane deaerator - Google Patents
Membrane deaeratorInfo
- Publication number
- JP3473866B2 JP3473866B2 JP17602394A JP17602394A JP3473866B2 JP 3473866 B2 JP3473866 B2 JP 3473866B2 JP 17602394 A JP17602394 A JP 17602394A JP 17602394 A JP17602394 A JP 17602394A JP 3473866 B2 JP3473866 B2 JP 3473866B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- degassing
- membrane
- water supply
- dissolved oxygen
- 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.)
- Expired - Lifetime
Links
Landscapes
- Degasification And Air Bubble Elimination (AREA)
- Physical Water Treatments (AREA)
- Removal Of Specific Substances (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、気液分離膜を使用して
水中から溶存酸素を除去する膜脱気装置に関するもので
ある。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a membrane deaerator for removing dissolved oxygen from water using a gas-liquid separation membrane.
【0002】[0002]
【従来の技術】近年、高層建築における水道水供給配管
の腐食が問題となっており、腐食を防止するため、給水
源に膜脱気装置を設置し、腐食の原因となる酸素を除去
した脱気水を給水することで腐食を防止するということ
が行われている。その場合、水の使用量は時間帯によっ
て大きく変動しているが、常に水を供給できるようにし
ておく必要があるため脱気装置は24時間の連続運転を
行っており、水使用量の少ない時間帯では無駄な運転を
行うことによる、ランニングコストの増大を招いてい
た。2. Description of the Related Art In recent years, corrosion of tap water supply pipes in high-rise buildings has become a problem, and in order to prevent corrosion, a membrane deaerator is installed at the water supply source to remove oxygen that causes corrosion. It is practiced to prevent corrosion by supplying steam. In that case, the amount of water used varies greatly depending on the time of day, but since it is necessary to always be able to supply water, the deaerator operates continuously for 24 hours, and the amount of water used is small. In a time zone, running costs are increased due to wasteful driving.
【0003】そのため、連絡管に積算流量計を挿入し、
水槽から給水配管への通水量が第1の設定値に達すると
脱気運転を開始し、給水配管より水槽への通水量が第2
の設定値に達すると脱気運転を停止するビル給水配管構
造における膜脱気装置の運転制御システム(特開5−2
28467)が提案されていた。このシステムでは水使
用量が少ない場合は脱気運転を停止させ、水槽に原水が
補給されて水槽内の溶存酸素濃度が上昇したころに脱気
運転を開始するものだが、水使用量が少ない場合に次回
脱気までの運転の間隔が長くなりすぎると、脱気水に酸
素が再溶解して溶存酸素濃度が上昇し、腐食を防止する
ことができなくなる。また、水使用量によって脱気運転
を行っているため、原水補給によって溶存酸素濃度が上
昇しても、そのまま給水されることがある。Therefore, an integrating flowmeter is inserted in the connecting pipe,
When the amount of water flowing from the water tank to the water supply pipe reaches the first set value, deaeration operation is started, and the amount of water flowing from the water supply pipe to the water tank reaches the second value.
Control system of the membrane degassing device in the building water supply piping structure that stops the degassing operation when the set value of
28467) was proposed. With this system, when the water usage is low, the degassing operation is stopped, and when the raw water is replenished to the water tank and the dissolved oxygen concentration in the water tank rises, the degassing operation is started, but when the water usage is low If the operation interval until the next degassing becomes too long, oxygen is redissolved in the degassed water, the dissolved oxygen concentration rises, and corrosion cannot be prevented. Further, since the degassing operation is performed depending on the amount of water used, even if the dissolved oxygen concentration rises due to raw water replenishment, water may be supplied as it is.
【0004】[0004]
【発明が解決しようとする課題】本発明が解決しようと
する課題は、給水配管の腐食を防ぎながら、無駄な脱気
運転を無くすことのできる膜脱気装置を提供することに
ある。SUMMARY OF THE INVENTION An object of the present invention is to provide a membrane deaerator capable of eliminating unnecessary deaerating operation while preventing corrosion of water supply piping.
【0005】[0005]
【課題を解決するための手段】原水を補給する原水供給
ラインが接続された水槽と、該原水供給ラインに設けら
れた補給装置と、真空発生装置を有する膜脱気モジュー
ルと、途中に循環ポンプが設けられ、前記水槽から膜脱
気モジュールへ送水する送水配管と、膜脱気モジュール
から水使用場所まで脱気水を給水する給水配管と、該給
水配管と水槽を接続する連結配管を設け、真空発生装置
および循環ポンプを作動させることによって脱気運転を
行う膜脱気装置において、タイマーを持ち、脱気運転を
所定間隔で行う運転制御装置を設け、脱気運転を所定間
隔で行う。Means for Solving the Problems A water tank to which a raw water supply line for replenishing raw water is connected, a replenishing device provided on the raw water supply line, a membrane degassing module having a vacuum generator, and a circulation pump in the middle of the tank. Is provided, a water supply pipe for supplying water from the water tank to the membrane degassing module, a water supply pipe for supplying degassed water from the membrane degassing module to a water use location, and a connection pipe for connecting the water supply pipe and the water tank, In a membrane degassing device that performs degassing operation by operating a vacuum generator and a circulation pump, an operation control device that has a timer and performs degassing operation at predetermined intervals is provided, and degassing operation is performed at predetermined intervals.
【0006】また、原水補給時や、脱気装置内適所に設
けた水中の溶存酸素濃度を検出する溶存酸素濃度計の検
出値が所定値以上であった場合に脱気運転を行い、溶存
酸素濃度が所定値以下となると脱気運転を停止する。In addition, when the raw water is replenished or when the value detected by a dissolved oxygen concentration meter for detecting the dissolved oxygen concentration in water provided at a proper position in the deaerator is above a predetermined value, the deaeration operation is performed to dissolve the dissolved oxygen. When the concentration becomes lower than the predetermined value, the degassing operation is stopped.
【0007】[0007]
【作用】所定間隔で脱気運転を行うこと、水槽への原水
補給時に脱気運転を行うこと、脱気装置内での水中の溶
存酸素濃度に応じて脱気運転を行うことにより、水使用
量が少ない時間帯での無駄な運転を防ぐことができ、か
つ溶存酸素濃度の上昇を防ぐことができる。時間で脱気
運転を制御している場合、脱気運転を停止することで水
の使用がない状態での無駄な運転を防ぐことができ、か
つ水の使用が無くても時間によって脱気運転を行うため
に、脱気装置内の溶存酸素濃度が上昇することを防ぐこ
とができる。また、水槽への原水補給時に脱気運転を行
う場合、原水補給によって水槽内の溶存酸素濃度は上昇
するが、脱気運転を行っていれば給水配管内には脱気処
理直後の脱気水を送ることになるので、給水配管内の溶
存酸素濃度は低い値を保つことができる。さらにまた、
溶存酸素濃度を検出し、溶存酸素濃度が所定値以上の場
合には所定値以下になるまで脱気運転を続行すること
で、確実に脱気することができる。[Operation] Water is used by performing deaeration operation at predetermined intervals, deaeration operation when replenishing raw water to the water tank, and deaeration operation according to the dissolved oxygen concentration in water in the deaerator. It is possible to prevent useless operation in a time zone when the amount is small, and to prevent an increase in dissolved oxygen concentration. When controlling the degassing operation by time, it is possible to prevent wasteful operation when water is not used by stopping the degassing operation, and even if there is no water used Therefore, it is possible to prevent the dissolved oxygen concentration in the deaerator from increasing. Also, when deaeration operation is performed when replenishing raw water to the water tank, the dissolved oxygen concentration in the water tank rises due to the replenishment of raw water, but if deaeration operation is performed, the deaeration water immediately after deaeration treatment will be placed in the water supply pipe. Therefore, the dissolved oxygen concentration in the water supply pipe can be kept at a low value. Furthermore,
By detecting the dissolved oxygen concentration and continuing the degassing operation until the dissolved oxygen concentration is equal to or higher than a predetermined value, the degassing can be reliably performed.
【0008】[0008]
【実施例】本発明の一実施例を図面を用いて説明する。
図1は膜脱気装置のフローであり、図2はタイムチャー
トを示している。水槽(1)内の水位を検出する水位検
出装置(9)によって水槽内水位が低下したことが出力
されたとき、原水を補給する原水供給ライン(13)の
途中に挿入された補給装置である補給水電磁弁(7)を
開き、一定の水位になるまで原水が補給される。水槽
(1)内に溜められた水は配管途中に、循環ポンプ
(3)が設けられた送水配管(4)を通り、真空発生装
置(11)に接続された膜脱気モジュール(5)に送ら
れて脱気処理が行われ、給水配管(6)によって各水使
用場所へ給水される。水中の溶存酸素濃度を検出する溶
存酸素濃度計(2)は、送水配管(4)に設けられた循
環ポンプ(3)の下流側から分岐され、該ポンプの上流
側に接続されたサンプル水配管(14)に設られる。こ
のサンプル水配管(14)を設けたことにより、従来溶
存酸素濃度計ごとに排出していた水を循環でき、無駄が
ない。給水配管(6)と水槽(1)は連結配管(10)
によって接続され、脱気運転停止中には水槽(1)内の
水が連結配管(10)および給水配管(6)を介して水
使用場所へ給水される。逆に、脱気運転中には給水配管
(6)を介して直接水使用場所へ給水され、余剰の脱気
水は水槽(1)内に連結配管(10)を介して戻され
る。運転制御装置(8)はインターバルタイマー(1
2)を持ち、循環ポンプ(3)、真空発生装置(1
1)、水位検出装置(9)、溶存酸素濃度計(2)のそ
れぞれに信号線で接続されている。さらに運転制御装置
(8)には、所定時間(例えば5分)の運転を継続する
所定脱気運転時間(A)、および所定の溶存酸素濃度
(例えば0.5ppm)が予め設定され、インターバルタイマ
ーには所定の時間(例えば3分)脱気運転を停止する脱
気運転停止時間(B)が設定されており、所定間隔で脱
気運転を行う。なお、この設定時間ならびに溶存酸素濃
度の設定値はこれに限られず任意でよい。例えば溶存酸
素濃度の設定値は腐食問題を生じない2ppm以下であ
ればどこに設定してもよい。An embodiment of the present invention will be described with reference to the drawings.
FIG. 1 shows the flow of the membrane degassing apparatus, and FIG. 2 shows a time chart. When the water level detecting device (9) for detecting the water level in the water tank (1) outputs that the water level in the water tank has dropped, the replenishing device is inserted in the middle of the raw water supply line (13) for replenishing the raw water. The make-up water solenoid valve (7) is opened, and raw water is replenished until it reaches a certain water level. The water accumulated in the water tank (1) passes through a water supply pipe (4) provided with a circulation pump (3) in the middle of the pipe, and then to a membrane degassing module (5) connected to a vacuum generator (11). The water is sent to be deaerated, and water is supplied to each water use place through the water supply pipe (6). A dissolved oxygen concentration meter (2) for detecting a dissolved oxygen concentration in water is branched from a downstream side of a circulation pump (3) provided in a water supply pipe (4), and a sample water pipe connected to an upstream side of the pump. It is installed in (14). By providing this sample water pipe (14), the water conventionally discharged for each dissolved oxygen concentration meter can be circulated and there is no waste. Connection pipe (10) between water supply pipe (6) and water tank (1)
The water in the water tank (1) is supplied to the place of use of water through the connecting pipe (10) and the water supply pipe (6) while the deaeration operation is stopped. On the contrary, during the deaeration operation, the water is directly supplied to the place where the water is used through the water supply pipe (6), and the surplus deaerated water is returned to the water tank (1) through the connection pipe (10). The operation control device (8) has an interval timer (1
2), circulation pump (3), vacuum generator (1
1), the water level detector (9), and the dissolved oxygen concentration meter (2) are connected by signal lines. Further, the operation control device (8) is preset with a predetermined degassing operation time (A) for continuing the operation for a predetermined time (for example, 5 minutes) and a predetermined dissolved oxygen concentration (for example, 0.5 ppm), and the interval timer is set. Is set to a deaeration operation stop time (B) for stopping the deaeration operation for a predetermined time (for example, 3 minutes), and the deaeration operation is performed at predetermined intervals. The set time and the set value of the dissolved oxygen concentration are not limited to this and may be arbitrary. For example, the set value of the dissolved oxygen concentration may be set to any value as long as it does not cause a corrosion problem and is 2 ppm or less.
【0009】水槽(1)内の水位が低下し、水位検出装
置(9)が原水補給信号を発信すると、補給水電磁弁
(7)が開かれ、原水補給が開始されると共に、運転制
御装置(8)は真空発生装置(11)、循環ポンプ
(3)を稼働させ、脱気運転を開始し、膜脱気装置の運
転時間を運転制御装置(8)内のタイマーでカウントす
る。原水補給によって水槽内溶存酸素濃度は上昇する
が、脱気運転を行っているので膜脱気モジュール(5)
で脱気処理された脱気処理された水が水使用場所へ直接
供給され、使用される。When the water level in the water tank (1) is lowered and the water level detection device (9) transmits a raw water replenishment signal, the replenishment water solenoid valve (7) is opened to start the raw water replenishment and the operation control device. In (8), the vacuum generator (11) and the circulation pump (3) are operated to start deaeration operation, and the operation time of the membrane deaeration device is counted by the timer in the operation control device (8). Although the dissolved oxygen concentration in the water tank increases due to the replenishment of raw water, the degassing operation is performed, so the membrane degassing module (5)
The degassed water degassed in (1) is directly supplied to the water use place and used.
【0010】以下図2をもとに説明する。水槽(1)内
の水位が上昇し、原水補給が終了後、タイマーによりカ
ウントした脱気運転時間が所定脱気運転時間(A)以上
でかつ溶存酸素濃度が予め設定された所定の濃度以下に
なると脱気運転を停止する(の状態)。これと同時に
インターバルタイマー(12)を作動させる。原水補給
が行われず、脱気運転が行われないまま、インターバル
タイマー(12)によって脱気運転停止時間(B)を経
過したことが出力されると、運転制御装置(8)は脱気
運転を開始する(の状態)。所定脱気運転時間(A)
の脱気運転を行った時点で溶存酸素濃度が所定溶存酸素
濃度以下であるときには脱気運転を停止するが、酸素再
溶解や原水補給によって所定脱気運転時間(A)の脱気
運転を行った後でも溶存酸素濃度が所定溶存酸素濃度を
越えるときにはさらに、溶存酸素濃度が所定値以下とな
るまで脱気運転を続行する(の状態)。また、水槽
(1)への原水補給信号が運転制御装置へ入力される
と、脱気運転停止時間(B)に関係なく脱気運転を開始
する(の状態)。A description will be given below with reference to FIG. After the water level in the water tank (1) rises and the supply of raw water is completed, the degassing operating time counted by the timer is equal to or longer than the predetermined degassing operating time (A) and the dissolved oxygen concentration is equal to or lower than the preset predetermined concentration. When this happens, the deaeration operation is stopped (state). At the same time, the interval timer (12) is activated. If the deaeration operation stop time (B) is output by the interval timer (12) without the raw water supply being performed and the deaeration operation not being performed, the operation control device (8) performs the deaeration operation. Start (state of). Specified degassing operation time (A)
When the dissolved oxygen concentration is equal to or lower than the predetermined dissolved oxygen concentration at the time of performing the degassing operation of, the degassing operation is stopped, but the degassing operation of the predetermined degassing operation time (A) is performed by re-dissolving oxygen and supplementing raw water. Even after the above, when the dissolved oxygen concentration exceeds the predetermined dissolved oxygen concentration, the degassing operation is further continued until the dissolved oxygen concentration becomes equal to or lower than the predetermined value (state). When the raw water supply signal to the water tank (1) is input to the operation control device, the deaeration operation is started regardless of the deaeration operation stop time (B) (state).
【0011】なお、本発明の好ましい態様として、以下
のものをあげることができる。溶存酸素濃度は送水配管
に設けられた循環ポンプ下流側から分岐され、該ポンプ
上流側に接続されたサンプル水配管に設けられているこ
とを特徴とする膜脱気装置。The following can be mentioned as preferred embodiments of the present invention. A dissolved oxygen concentration is branched from a circulation pump downstream side provided in a water supply pipe, and is provided in a sample water pipe connected to the pump upstream side.
【0012】[0012]
【発明の効果】溶存酸素濃度の高い水が供給されること
無く、かつ脱気運転が無用な場合には脱気運転を停止す
ることができるので、膜脱気装置のランニングコストを
抑え、効率的な運転を行うことができ、腐食防止効果は
維持することができる。The degassing operation can be stopped when the water with a high dissolved oxygen concentration is not supplied and the degassing operation is unnecessary, so that the running cost of the membrane degassing apparatus can be suppressed and the efficiency can be improved. Operation can be performed, and the corrosion prevention effect can be maintained.
【図1】 本発明の一実施例のフローシートFIG. 1 is a flow sheet of an embodiment of the present invention.
【図2】 本発明の一実施例のタイムチャートFIG. 2 is a time chart of an embodiment of the present invention.
1 水槽 2 溶存酸素濃度計 3 循環ポンプ 4 送水配管 5 膜脱気モジュール 6 給水配管 7 補給装置(補給水電磁弁) 8 運転制御装置 9 水位検出装置 10 連結配管 11 真空発生装置 12 インターバルタイマー 13 原水供給ライン 14 サンプル水配管 A 所定脱気運転時間 B 脱気運転間隔時間 1 aquarium 2 Dissolved oxygen concentration meter 3 circulation pumps 4 water supply piping 5 Membrane degassing module 6 water supply piping 7 Replenishment device (make-up water solenoid valve) 8 Operation control device 9 Water level detector 10 connection piping 11 Vacuum generator 12 Interval timer 13 Raw water supply line 14 sample water piping A specified degassing operation time B degassing operation interval time
フロントページの続き (72)発明者 小澤 芳弘 東京都新宿区西新宿3丁目4番7号栗田 工業株式会社内 (56)参考文献 特開 平6−79259(JP,A) 実開 平4−137705(JP,U) 実用新案登録3003429(JP,U) (58)調査した分野(Int.Cl.7,DB名) C02F 1/20 C02F 1/00 B01D 19/00 - 19/04 Front page continuation (72) Inventor Yoshihiro Ozawa 3-4-7 Nishishinjuku, Shinjuku-ku, Tokyo Kurita Industry Co., Ltd. (56) Reference JP-A-6-79259 (JP, A) Mitsuihei 4-137705 (JP, U) Utility model registration 3003429 (JP, U) (58) Fields investigated (Int.Cl. 7 , DB name) C02F 1/20 C02F 1/00 B01D 19/00-19/04
Claims (3)
れた水槽と、該原水供給ラインに設けられた補給装置
と、真空発生装置を有する膜脱気モジュールと、途中に
循環ポンプが設けられ、前記水槽から膜脱気モジュール
へ送水する送水配管と、膜脱気モジュールから水使用場
所まで脱気水を給水する給水配管と、給水配管と水槽を
接続する連結配管を設け、真空発生装置および循環ポン
プを作動させることによって脱気運転を行う膜脱気装置
において、脱気運転を所定間隔で行う運転制御装置を設
けたことを特徴とする膜脱気装置。1. A water tank to which a raw water supply line for replenishing raw water is connected, a replenishing device provided on the raw water supply line, a membrane degassing module having a vacuum generator, and a circulation pump provided midway, A water supply pipe for supplying water from the water tank to the membrane degassing module, a water supply pipe for supplying degassed water from the membrane degassing module to a place where water is used, and a connecting pipe connecting the water supply pipe and the water tank are provided, and a vacuum generator and a circulation system are provided. A membrane degassing apparatus that performs degassing operation by operating a pump , comprising an operation control device that performs degassing operation at predetermined intervals .
運転制御装置は原水補給時にも脱気運転を行うものであ
ることを特徴とする膜脱気装置。 2. The membrane degassing apparatus according to claim 1,
The operation control device performs deaeration operation even when replenishing raw water.
A membrane degassing device characterized in that
おいて、運転制御装置は原水補給時もしくは所定間隔で
脱気運転を行うと共に、脱気装置内適所に設けられた水
中の溶存酸素濃度を検出する溶存酸素濃度計の検出値が
所定値以下であった場合脱気運転を停止し、所定値以上
であった場合、所定値以下になるまで脱気運転を続行す
るよう運転制御するものであることを特徴とする膜脱気
装置。3. The membrane degassing apparatus according to claim 1 or 2 , wherein the operation control device performs degassing operation at the time of replenishing raw water or at predetermined intervals, and dissolves oxygen in water provided in a proper place in the degassing apparatus. If the detected value of the dissolved oxygen concentration meter that detects the concentration is less than or equal to a predetermined value, deaeration operation is stopped, and if it is greater than or equal to a predetermined value, operation control is performed to continue the deaeration operation until it falls below a predetermined value Membrane deaerator characterized by being a thing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17602394A JP3473866B2 (en) | 1994-07-04 | 1994-07-04 | Membrane deaerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17602394A JP3473866B2 (en) | 1994-07-04 | 1994-07-04 | Membrane deaerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0810749A JPH0810749A (en) | 1996-01-16 |
| JP3473866B2 true JP3473866B2 (en) | 2003-12-08 |
Family
ID=16006379
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17602394A Expired - Lifetime JP3473866B2 (en) | 1994-07-04 | 1994-07-04 | Membrane deaerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3473866B2 (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20020078720A (en) * | 2001-04-10 | 2002-10-19 | 주식회사 코오롱 | Temperature sensitive solar control film |
| JP4899635B2 (en) * | 2006-05-25 | 2012-03-21 | 三浦工業株式会社 | Deoxygenation system |
| JP4899636B2 (en) * | 2006-05-25 | 2012-03-21 | 三浦工業株式会社 | Oxygen absorber |
| JP5071034B2 (en) * | 2007-10-18 | 2012-11-14 | 三浦工業株式会社 | Boiler degassing water supply system |
| JP6617071B2 (en) * | 2016-04-20 | 2019-12-04 | オルガノ株式会社 | Pure water production method and apparatus |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3003429U (en) | 1994-04-22 | 1994-10-18 | 株式会社サンワード | Deaerator |
-
1994
- 1994-07-04 JP JP17602394A patent/JP3473866B2/en not_active Expired - Lifetime
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3003429U (en) | 1994-04-22 | 1994-10-18 | 株式会社サンワード | Deaerator |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0810749A (en) | 1996-01-16 |
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