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JPH06181B2 - ▲ Ro ▼ Backwash method of excess equipment - Google Patents

▲ Ro ▼ Backwash method of excess equipment

Info

Publication number
JPH06181B2
JPH06181B2 JP60034626A JP3462685A JPH06181B2 JP H06181 B2 JPH06181 B2 JP H06181B2 JP 60034626 A JP60034626 A JP 60034626A JP 3462685 A JP3462685 A JP 3462685A JP H06181 B2 JPH06181 B2 JP H06181B2
Authority
JP
Japan
Prior art keywords
line
liquid
air
drain
scrubbing
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
Application number
JP60034626A
Other languages
Japanese (ja)
Other versions
JPS61197005A (en
Inventor
真策 丸山
隆夫 猪野
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP60034626A priority Critical patent/JPH06181B2/en
Publication of JPS61197005A publication Critical patent/JPS61197005A/en
Publication of JPH06181B2 publication Critical patent/JPH06181B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

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  • Filtration Of Liquid (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は過装置、特に中空糸膜を用いた過装置で膜
の通気性が悪い場合に有効な逆洗方法に関する。
Description: TECHNICAL FIELD The present invention relates to a perfusator, and more particularly to a backwashing method which is effective when a hollow fiber membrane has a poor air permeability.

〔従来の技術及びその問題点〕[Conventional technology and its problems]

中空糸膜を用いた過装置における従来行われていた逆
洗方法を第1図に基いて説明する。
A backwashing method which has been conventionally performed in a filtration apparatus using a hollow fiber membrane will be described with reference to FIG.

被処理液タンク1中の被処理液をポンプ2により流量調
節弁3を介して流量を調節しながら給液ライン8を経て
分配機構6から過装置4に供給し、供給された被処理
液は過装置中を上向きに流れ、過メデイア5で過
された後、処理液(液)は管板上部のドームを経て処
理液ライン9から排出される。被処理水の過処理を行
つている間、差圧検出器DPにより差圧(過抵抗)を
測定し、差圧が一定値以上となった場合、被処理液の供
給を止め、処理液ライン9を閉とした後逆洗が行なわれ
る。
The liquid to be treated in the liquid to be treated tank 1 is supplied from the distribution mechanism 6 to the excess device 4 via the liquid supply line 8 while the flow rate is adjusted by the pump 2 via the flow rate adjusting valve 3, and the supplied liquid to be treated is After flowing upward through the filter and passing through the media 5, the processing liquid (liquid) is discharged from the processing liquid line 9 through the dome above the tube sheet. During the overtreatment of the water to be treated, the differential pressure (over resistance) is measured by the differential pressure detector DP, and when the differential pressure exceeds a certain value, the supply of the liquid to be treated is stopped and the treatment liquid line After closing 9, the backwash is performed.

逆洗を空気を用いて行う場合には、ドームドレンライン
14から過装置4の上部のドーム液を排出した後加圧
空気ライン12からの空気で加圧し、内包液を逆洗液排
出ライン16より一気に排出した後、液張りライン11
から液が管板に達するまで液張りし、ついでスクラビン
グ用空気ライン13から給液ライン8を経て分配機構6
から過装置4に空気を導入し、過メデイアを空気ス
クラビングした後逆洗液排出液ライン16から排液し、
ついで液張りライン10及び11から導入して液張りす
る。なお、中空糸膜の通気性が良好な場合には、空気ス
クラビングは省略してもよい。
When backwashing is performed by using air, the dome liquid on the upper part of the apparatus 4 is discharged from the dome drain line 14 and then pressurized from the pressurized air line 12 to pressurize the inclusion liquid to the backwash liquid discharge line 16. After discharging all at once, the liquid filling line 11
Liquid is filled until it reaches the tube sheet, and then the scrubbing air line 13 passes through the liquid supply line 8 and the distribution mechanism 6
Air is introduced into the excess device 4, the excess media is scrubbed with air, and then drained from the backwash liquid drain line 16,
Then, it is introduced from the liquid filling lines 10 and 11 to fill the liquid. If the hollow fiber membrane has good air permeability, air scrubbing may be omitted.

一方、液のみを用いて逆洗を行う場合(中空糸膜の空気
透過性が悪い場合)には、逆洗用液ライン10より逆洗
用液を圧入し、ほぼ過装置4の管板下部までの液を逆
洗液排液ライン16から一気に排液し、ついでスクラビ
ング時開放ライン15を開とすると共にスクラビング空
気ライン13から給液ライン8及び分配機構6を経て空
気を過装置に導入し、過メデイア5を空気スクラビ
ングした後逆洗排液ライン16から排液し、ついで液張
りライン10及び11から液を導入して液張りする。
On the other hand, when backwashing is performed using only the liquid (when the air permeability of the hollow fiber membrane is poor), the backwashing liquid is press-fitted from the backwashing liquid line 10 to almost the lower part of the tube plate of the apparatus 4. The liquid up to is drained all at once from the backwash liquid drain line 16, then the opening line 15 is opened at the time of scrubbing, and the air is introduced from the scrubbing air line 13 through the liquid feed line 8 and the distribution mechanism 6 into the excess device. After air scrubbing the excess medium 5, liquid is drained from the backwash drain line 16, and then liquid is introduced from the liquid fill lines 10 and 11 to fill the liquid.

上記の逆洗においては、前者、後者いずれの方法をとつ
た場合にも逆洗工程時に生ずる廃液量は過装置4の内
包液量の2倍近くになるので廃液低減対策上は好ましく
ない。
In both cases of the former and latter methods in the above backwashing, the amount of waste liquid generated during the backwashing process is close to twice the amount of the liquid contained in the excess device 4, which is not preferable in terms of waste liquid reduction measures.

〔発明の構成〕[Structure of Invention]

本発明は、 過装置の逆洗を行う方法において、 (イ) 加圧空気ラインを開としドームドレンラインを介
して過装置のドームドレンを行い、 (ロ) ついでドームドレンラインを閉とし、加圧空気ラ
インから空気を供給してドーム内を加圧し、ドーム内の
空気が所定圧力に達した後加圧空気ラインを閉とし、 (ハ) 逆洗液排液ラインを開として排出液が管板の下部
に達し逆洗液排液ラインが液切れとなるまで液の排出を
行うか、または、逆洗液排液ラインを同時に開とし、逆
洗液排液ラインは瞬時に閉とし、排出液が管板の下部に
達し逆洗液排液ラインが液切れとなるまで液の排出を行
つた後、 (ニ) スクラビング用空気ラインを開とし、給液ライン
を経て分配機構から空気を供給し、スクラビング時開放
ラインから空気を排気しながら過装置内の過メデイ
アを所定時間空気スクラビングし、次いで (ホ) スクラビング用空気ラインを閉とし、ドレンライ
ンを開として、逆洗液を全て排出した後ドレンライン及
びスクラビング時開放ラインを閉とする ことを特徴とする過装置の逆洗方法 であつて、空気スクラビング前に過装置4中に内包す
る液の排出を行なわないので、逆洗工程中に発生する廃
液量はほゞ過装置4内に内包されている液量だけとな
り、従来法に比し廃液量は約1/2となり廃液対策上有利
となる。
The present invention relates to a method for backwashing an excess device, (a) opening the pressurized air line and performing the dome drain of the excess device through the dome drain line, and (b) then closing the dome drain line and applying Air is supplied from the compressed air line to pressurize the inside of the dome, and after the air inside the dome reaches the specified pressure, the pressurized air line is closed, and (c) the backwash liquid drain line is opened and the discharged liquid is piped. Drain the liquid until it reaches the bottom of the plate and the backwash liquid drain line runs out, or open the backwash liquid drain line at the same time and immediately close the backwash liquid drain line and drain. After the liquid reaches the bottom of the tube plate and drains the backwash liquid drain line until the liquid runs out, (d) Open the scrubbing air line and supply air from the distribution mechanism via the liquid supply line. When scrubbing, exhaust air from the open line while The air is scrubbed for a predetermined time, and then (e) the scrubbing air line is closed, the drain line is opened, and after draining all the backwash liquid, the drain line and the scrubbing open line are closed. This is a backwashing method for the overwashing device, and since the liquid contained in the overwashing device 4 is not discharged before the air scrubbing, the amount of waste liquid generated during the backwashing process is included in the overwashing device 4. Only the amount of liquid is used, and the amount of waste liquid is about half that of the conventional method, which is advantageous in terms of waste liquid countermeasures.

逆洗が終つた後は、液張りライン11から液を過装置
4に導入し、過メデイア5を支えている下部管板まで
液が達し、管板空気抜きライン15から液が出はじめた
ら管板空気抜きライン15及び液張りライン11を閉と
する。ついで、ペント17及び液張りライン10を開と
し、液張りライン10から液を過装置の上部へ導入
し、ベント17から液が出はじめたら、ベント17及び
液張りライン10を閉とし、処理液ライン9を開とした
後被処理液タンクから被処理液を導入して被処理液の処
理を再開する。
After the backwashing is completed, the liquid is introduced from the liquid filling line 11 into the excess device 4 and reaches the lower tube sheet supporting the excess medium 5, and when the solution begins to come out from the tube sheet air vent line 15, the tube sheet is released. The air vent line 15 and the liquid filling line 11 are closed. Then, the pent 17 and the liquid filling line 10 are opened, the liquid is introduced from the liquid filling line 10 to the upper part of the apparatus, and when the liquid begins to come out from the vent 17, the vent 17 and the liquid filling line 10 are closed, and the treatment liquid After opening the line 9, the liquid to be treated is introduced from the liquid to be treated tank and the treatment of the liquid to be treated is restarted.

ところで、上記(ハ)の工程において、逆洗液排液ライン
15の口径が逆洗液排液ライン16の口径と同程度であ
つて十分に大きい場合には、逆洗液排液ライン15から
のみ液の排出を行えばよい。
By the way, in the above step (c), if the diameter of the backwash liquid drain line 15 is about the same as the diameter of the backwash liquid drain line 16 and is sufficiently large, Only the liquid should be discharged.

しかしながら、第1図Aで示す部分のように過装置内
の逆洗液排液ライン取り付け部に立上がりが必要であつ
たり、或いは管板部に逆洗排液ライン15に導く穴をあ
ける場合、前者は過面積の確保という観点から、後者
は穴が大きいと管板が厚くなつてしまうので、逆洗液排
液ライン15の口径は大きくすることはできないため、
逆洗液排液ライン15の口径は一般に逆洗液排液ライン
16の口径よりも小さいことが多い。その結果逆洗液排
液ライン15における逆洗時の圧力損失は可成大きくな
り、逆洗時の過材面間差圧が十分にとれない恐れがあ
る。
However, when the backwashing liquid drainage line mounting portion in the apparatus needs to be raised as shown in FIG. 1A, or when a hole for leading to the backwashing liquid drainage line 15 is formed in the tube plate portion, In the former case, from the viewpoint of securing an excessive area, in the latter case, if the hole is large, the tube plate becomes thick, and therefore the diameter of the backwash liquid drainage line 15 cannot be increased.
The backwash liquid drainage line 15 generally has a smaller diameter than the backwash liquid drainage line 16. As a result, the pressure loss during backwashing in the backwashing liquid drain line 15 becomes considerably large, and there is a risk that the pressure difference between the excess material surfaces during backwashing may not be sufficient.

この場合、逆洗排液ライン16も瞬時開とし材面間の
差圧を確保して材に衝撃を与えた後閉とし、逆洗液排
液ラインが液切れとなるまで過装置上部の液を排液す
る。
In this case, the backwash drainage line 16 is also opened instantaneously, the pressure difference between the material surfaces is secured, the material is shocked, and then closed. Drain.

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

第1図は、本発明で用いる過装置の一例を示すフロー
図である。 1・・被処理液タンク、2・・供給ポンプ、4・・過
装置、5・・過メデイア、6・・分配機構、7・・逆
洗受タンク、8・・給液ライン、9・・処理液ライン、
10・・逆洗液用兼液張りライン、11・・液張りライ
ン、12・・加圧空気ライン、13・・スクラビング用
空気ライン、14・・ドームドレンライン、15・・管
板空気抜きライン兼スクラビング時開放ライン兼逆洗液
排液ライン、16・・逆洗液排液ライン兼ドレンライ
ン、17・・ベント
FIG. 1 is a flow chart showing an example of a transit device used in the present invention. 1 ・ ・ Processed liquid tank, 2 ・ ・ Supply pump, 4 ・ ・ Over device, 5 ・ ・ Over media, 6 ・ ・ Distribution mechanism, 7 ・ ・ Backwash receiving tank, 8 ・ ・ Liquid supply line, 9 ・ ・Processing liquid line,
10 ··· Backwashing liquid combined liquid filling line, 11 ··· Liquid filling line, 12 · · Pressurized air line, 13 · · Scrubbing air line, 14 · · Dome drain line, 15 · · Tube plate air vent line Open line for scrubbing and backwash liquid drainage line, 16 ・ ・ Backwash liquid drainage line and drain line, 17 ・ ・ Vent

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】過装置の逆洗を行う方法において、 (イ) 加圧空気ライン(12)を開としドームドレンライ
ン(14)を介して過装置4のドームドレンを行い、 (ロ) ついでドームドレンライン(14)を閉とし、加圧
空気ライン(12)から空気を供給してドーム内を加圧
し、ドーム内の空気が所定圧力に達した後加圧空気ライ
ン(12)を閉とし、 (ハ) 逆洗液排液ライン(15)を開として排出液が管板
の下部に達し逆洗液排液ライン(15)が液切れとなるま
で液の排出を行うか、または、逆洗液排液ライン15及
び16を同時に開とし、逆洗液排液ライン(16)は瞬時
に閉とし、排出液が管板の下部に達し逆洗液排液ライン
(15)が液切れとなるまで液の排出を行つた後、 (ニ) スクラビング用空気ライン(13)を開とし、給液
ライン(8)を経て分配機構から空気を供給し、スクラ
ビング時開放ライン(15)から空気を排気しながら過
装置(4)内の過メデイアを所定時間空気スクラビン
グし、次いで、 (ホ) スクラビング用空気ライン(13)を閉とし、ドレ
ンライン(16)を開として逆洗液を全て排出した後ドレ
ンライン(16)及びスクラビング時開放ライン(15)を
閉とする ことを特徴とする過装置の逆洗方法。
1. A method of backwashing an over-apparatus, comprising: (a) opening a pressurized air line (12) and performing a dome drain of the over-apparatus 4 via a dome drain line (14); Close the dome drain line (14), supply air from the pressurized air line (12) to pressurize the dome, and close the pressurized air line (12) after the air in the dome reaches a predetermined pressure. , (C) Open the backwash liquid drain line (15) and discharge the liquid until the drain reaches the bottom of the tube plate and the backwash liquid drain line (15) runs out, or The washing liquid drain lines 15 and 16 are simultaneously opened, the backwash liquid drain line (16) is instantly closed, and the drainage liquid reaches the lower part of the tube plate and the backwash liquid drainage line (15) runs out of liquid. After the liquid has been discharged until (4), the air line (13) for scrubbing is opened, and the distribution mechanism (8) is opened via the liquid supply line (8). While supplying air and exhausting air from the open line (15) during scrubbing, air scrubbing the excess media in the device (4) for a predetermined time, and then (e) closing the scrubbing air line (13), A method for backwashing an over-apparatus characterized in that the drain line (16) is opened, all the backwash liquid is discharged, and then the drain line (16) and the scrubbing open line (15) are closed.
JP60034626A 1985-02-25 1985-02-25 ▲ Ro ▼ Backwash method of excess equipment Expired - Lifetime JPH06181B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60034626A JPH06181B2 (en) 1985-02-25 1985-02-25 ▲ Ro ▼ Backwash method of excess equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60034626A JPH06181B2 (en) 1985-02-25 1985-02-25 ▲ Ro ▼ Backwash method of excess equipment

Publications (2)

Publication Number Publication Date
JPS61197005A JPS61197005A (en) 1986-09-01
JPH06181B2 true JPH06181B2 (en) 1994-01-05

Family

ID=12419599

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60034626A Expired - Lifetime JPH06181B2 (en) 1985-02-25 1985-02-25 ▲ Ro ▼ Backwash method of excess equipment

Country Status (1)

Country Link
JP (1) JPH06181B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001129369A (en) * 1999-11-08 2001-05-15 Japan Organo Co Ltd Method for cleaning of hollow fiber membrane and hollow fiber membrane filter

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61274709A (en) * 1985-05-29 1986-12-04 Ebara Corp Hollow yarn membrane filter apparatus
US5639373A (en) 1995-08-11 1997-06-17 Zenon Environmental Inc. Vertical skein of hollow fiber membranes and method of maintaining clean fiber surfaces while filtering a substrate to withdraw a permeate
US7087173B2 (en) 1995-08-11 2006-08-08 Zenon Environmental Inc. Inverted cavity aerator for membrane module
DE69633806T2 (en) 1995-08-11 2005-05-12 Zenon Environmental Inc., Oakville Device for removing permeate from a liquid substrate with several components
ATE292511T1 (en) 1998-11-23 2005-04-15 Zenon Environmental Inc WATER FILTRATION USING UNDERWATER MEMBRANES
EP2801399A1 (en) * 2013-05-07 2014-11-12 Siemens Aktiengesellschaft Compact multi membrane vessel for water ultrafiltration

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001129369A (en) * 1999-11-08 2001-05-15 Japan Organo Co Ltd Method for cleaning of hollow fiber membrane and hollow fiber membrane filter
JP4570714B2 (en) * 1999-11-08 2010-10-27 オルガノ株式会社 Hollow fiber membrane cleaning method and hollow fiber membrane filtration device

Also Published As

Publication number Publication date
JPS61197005A (en) 1986-09-01

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