JPH0985065A - Membrane separation treatment apparatus - Google Patents

Membrane separation treatment apparatus

Info

Publication number
JPH0985065A
JPH0985065A JP24928095A JP24928095A JPH0985065A JP H0985065 A JPH0985065 A JP H0985065A JP 24928095 A JP24928095 A JP 24928095A JP 24928095 A JP24928095 A JP 24928095A JP H0985065 A JPH0985065 A JP H0985065A
Authority
JP
Japan
Prior art keywords
membrane
water tank
raw water
module
raw
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.)
Granted
Application number
JP24928095A
Other languages
Japanese (ja)
Other versions
JP3310836B2 (en
Inventor
Masayoshi Kaga
正悦 加賀
Katsumi Cho
克美 長
Hiroshi Mizutani
洋 水谷
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP24928095A priority Critical patent/JP3310836B2/en
Publication of JPH0985065A publication Critical patent/JPH0985065A/en
Application granted granted Critical
Publication of JP3310836B2 publication Critical patent/JP3310836B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PROBLEM TO BE SOLVED: To wash a membrane module with chemicals without taking the same out of an aeration tank in a membrane separation treatment apparatus using the membrane module separating a contaminant from membrane raw water. SOLUTION: A membrane water tank 1 housing a membrane module 2 is provided separately from a membrane raw water tank 10 and connected to the membrane raw water tank 10 through a circulating device 3. The membrane raw water 5 in the membrane raw water tank 10 sent to the membrane water tank 1 by the circulating device 3 is taken out as treated water 4 while a pollutant in the raw water 5 is separated by the membrane module 2. When the membrane module 2 in the membrane water tank 1 is washed with a washing soln. 5', the liquid in the membrane water tank 1 is replaced with the washing soln. 5' to wash the membrane module 2 without taking out the same.

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、水処理装置におい
て、膜原水から汚濁物質を分離するのに膜モジュールを
用いた膜分離処理装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water treatment apparatus, which uses a membrane module to separate pollutants from raw membrane water.

【0002】[0002]

【従来の技術】図3に示すように汚濁物質を分離する為
に膜モジュール2を膜原水槽(曝気槽)8内に設置した
膜分離処理装置ではその膜モジュール2の下部に散気管
9を設け、曝気することにより膜原水槽(曝気槽)8内
に流れを与え、膜表面に付着した濾過物を洗浄する効果
を得ていた。
2. Description of the Related Art As shown in FIG. 3, in a membrane separation treatment apparatus in which a membrane module 2 is installed in a membrane raw water tank (aeration tank) 8 for separating pollutants, an air diffuser 9 is provided below the membrane module 2. By providing and aerating, a flow is given into the membrane raw water tank (aeration tank) 8 to obtain the effect of cleaning the filtered substance adhering to the membrane surface.

【0003】一方、膜モジュール2を薬品等により洗浄
する場合は、膜原水槽(曝気槽)8の外へ膜モジュール
2を取り出し、人手による洗浄を行っていた為に不衛生
であった。
On the other hand, when the membrane module 2 is washed with chemicals or the like, it is unsanitary because the membrane module 2 is taken out of the raw membrane water tank (aeration tank) 8 and manually washed.

【0004】[0004]

【発明が解決しようとする課題】前記したように、膜モ
ジュールを用いた従来の膜分離処理装置では、膜モジュ
ール2を曝気槽8内に直接設置している為、膜モジュー
ル2を薬品等で膜洗浄する場合、膜モジュール2を膜原
水槽8外に取り出し、人手による洗浄や、別に設置した
洗浄用のタンクに移送し、洗浄しなければならなかっ
た。
As described above, in the conventional membrane separation treatment apparatus using the membrane module, the membrane module 2 is directly installed in the aeration tank 8, so that the membrane module 2 can be exposed to chemicals or the like. In the case of membrane cleaning, the membrane module 2 had to be taken out of the membrane raw water tank 8 and manually washed, or transferred to a separately installed tank for washing and washed.

【0005】そこで本発明は、膜原水から汚濁物質を分
離するための膜モジュールを用いた膜分離処理装置にお
いて、膜モジュールを膜原水槽(曝気槽)外へ取り出す
ことなく、しかも人手によらないで薬品等による洗浄を
行えるようにした膜分離処理装置を提供することを課題
としている。
In view of this, the present invention is a membrane separation treatment apparatus using a membrane module for separating pollutants from raw membrane water, without taking the membrane module out of the raw membrane water tank (aeration tank) and without human labor. It is an object of the present invention to provide a membrane separation treatment device capable of cleaning with chemicals or the like.

【0006】[0006]

【課題を解決するための手段】本発明は、膜原水から汚
濁物質を分離する膜モジュールを用いた膜分離処理装置
における前記課題を解決するため、膜モジュールを内部
に収納すると共に内部に膜原水を流出入させるように構
成した膜水槽を設けた構成を採用する。
In order to solve the above-mentioned problems in a membrane separation treatment apparatus using a membrane module for separating pollutants from membrane raw water, the present invention accommodates the membrane module inside the membrane raw water. Adopting a configuration provided with a membrane water tank configured to flow in and out.

【0007】本発明で用いる前記膜水槽としては、散気
管を底部に設けた膜原水槽と別に設置し、その膜原水槽
から膜原水の供給を受けてその膜原水が膜水槽内を循環
して流れるように構成することができる。
The membrane water tank used in the present invention is installed separately from the membrane raw water tank having an air diffusing pipe at the bottom, and the membrane raw water is supplied from the membrane raw water tank to circulate in the membrane water tank. Can be configured to flow.

【0008】このように構成した膜水槽を用いることに
より膜水槽内に膜原水槽から膜原水を供給して、膜水槽
内を循環させ、内部に設置された膜モジュールを膜原水
が流通することによって膜面への固形物の付着を防止し
つつ膜原水中の汚濁物質を分離除去することができる。
By using the membrane water tank configured as described above, the membrane raw water is supplied from the membrane raw water tank into the membrane water tank, circulates in the membrane water tank, and the membrane raw water flows through the membrane module installed inside. By doing so, it is possible to separate and remove pollutants in the raw water of the membrane while preventing solids from adhering to the membrane surface.

【0009】また、膜モジュールを薬品等で洗浄すると
きは、その膜水槽内の膜原水を洗浄液と置換可能に構成
し、膜水槽内を洗浄液が流れるように循環させることに
より膜モジュールの洗浄を行うことができる。
When cleaning the membrane module with chemicals, the membrane raw water in the membrane water tank can be replaced with the cleaning liquid, and the membrane module is cleaned by circulating the cleaning liquid so that the cleaning liquid flows. It can be carried out.

【0010】或いはまた、本発明で用いる前記膜水槽
は、散気管を底部に設けた膜原水槽内に配置し、その膜
水槽に膜原水の流入口、流出口を設けた構成とすること
ができる。
Alternatively, the membrane water tank used in the present invention may be arranged in a membrane raw water tank having an air diffuser at the bottom, and the membrane water tank may be provided with an inlet and an outlet of the raw membrane water. it can.

【0011】このように構成した膜水槽を用いることに
よって膜水槽内にはその流入口、流出口を通して膜原水
槽内の膜原水を流通させて膜モジュールの膜面への固形
物の付着を防止しつつ膜モジュールによる汚濁物質の除
去を行わせることができる。また、膜モジュールを洗浄
液で洗浄するときは、膜水槽内の膜原水を洗浄液と置換
可能に構成することにより、膜水槽内の液を置換させて
洗浄を行えばよい。
By using the membrane water tank configured as described above, the membrane raw water in the membrane raw water tank is circulated through the membrane water tank through its inflow port and outflow port to prevent solid matter from adhering to the membrane surface of the membrane module. Meanwhile, the contaminants can be removed by the membrane module. Further, when the membrane module is washed with the washing liquid, the raw membrane water in the membrane water tank can be replaced with the washing liquid so that the liquid in the membrane water tank is replaced with the washing liquid.

【0012】以上のように、本発明による膜分離処理装
置では膜原水槽(曝気槽)と分離された膜水槽を設け、
膜モジュールの洗浄はその膜水槽内で行える為、洗浄時
の膜モジュールの引上げ作業、手作業による洗浄等の不
衛生作業が不要となる。
As described above, the membrane separation apparatus according to the present invention is provided with the membrane water tank separated from the membrane raw water tank (aeration tank),
Since the membrane module can be washed in the membrane water tank, unsanitary work such as pulling up the membrane module and washing by hand during cleaning is unnecessary.

【0013】また、本発明による膜分離処理装置では、
膜水槽内の膜原水を水又は液体に置換することにより、
別置の洗浄装置、タンク等を必要とせずに膜モジュール
の洗浄を行える。
Further, in the membrane separation treatment apparatus according to the present invention,
By replacing the raw membrane water in the membrane water tank with water or liquid,
The membrane module can be cleaned without the need for a separate cleaning device, tank, etc.

【0014】[0014]

【発明の実施の形態】以下、本発明による膜分離処理装
置について図1、図2に示した実施の形態に基づいて具
体的に説明する。なお、以下の実施の形態において、図
3に示した従来の装置と同じ構成の部分には説明を簡単
にするため同じ符号を付してある。
BEST MODE FOR CARRYING OUT THE INVENTION A membrane separation treatment apparatus according to the present invention will be specifically described below based on the embodiment shown in FIGS. In the following embodiments, parts having the same configurations as those of the conventional device shown in FIG. 3 are designated by the same reference numerals for simplification of description.

【0015】(実施の第1形態)まず、図1に示した本
発明の実施の第1形態について説明する。図1におい
て、1は膜水槽で、内部に膜モジュール2が収納されて
いる。10は膜原水槽で、その底部には散気管9が設け
られている。膜水槽1は、膜原水槽10とポンプ等の循
環装置3を介して連絡されている。5′は膜モジュール
2を洗浄するための洗浄液である。
(First Embodiment) First, the first embodiment of the present invention shown in FIG. 1 will be described. In FIG. 1, 1 is a membrane water tank in which a membrane module 2 is housed. A membrane raw water tank 10 is provided with an air diffuser 9 at the bottom thereof. The membrane water tank 1 is connected to the membrane raw water tank 10 via a circulation device 3 such as a pump. 5'is a cleaning liquid for cleaning the membrane module 2.

【0016】膜水槽1を出る循環水は、膜原水のときは
膜原水槽10へ、洗浄液の場合は循環装置3の流入側へ
循環される。4は、膜モジュール2を通過して取り出さ
れる処理水を示している。
The circulating water exiting the membrane water tank 1 is circulated to the membrane raw water tank 10 when the membrane raw water is used, and to the inflow side of the circulation device 3 when the washing liquid is used. Reference numeral 4 denotes treated water that is taken out through the membrane module 2.

【0017】このように構成された図1の膜分離処理装
置において、通常の運転時は、膜原水槽10内の膜原水
5を循環装置3によって膜水槽1に供給し膜モジュール
2の表面を通過させた循環水6が得られる。循環水6は
図示の膜原水槽10等に戻される。
In the membrane separation treatment apparatus of FIG. 1 thus constructed, during normal operation, the raw membrane water 5 in the raw membrane water tank 10 is supplied to the membrane water tank 1 by the circulation device 3 to clean the surface of the membrane module 2. The passed circulating water 6 is obtained. The circulating water 6 is returned to the membrane raw water tank 10 shown in the figure.

【0018】また、膜モジュール2を膜原水5とは別の
洗浄液によって洗浄する時は、洗浄液5′を循環装置3
により膜水槽1に供給し、膜モジュール2の表面を通過
して洗浄後の循環水6は、循環装置3の入口に戻され再
び循環される。
When the membrane module 2 is washed with a washing liquid different from the raw membrane water 5, the washing liquid 5'is circulated.
The circulating water 6 after being supplied to the membrane water tank 1 through the surface of the membrane module 2 after cleaning is returned to the inlet of the circulation device 3 and circulated again.

【0019】即ち、循環水6は膜水槽1内を、何度も通
過してしばらく循環し、汚れた循環水6はバルブ(図示
していない)を切り換えることにより、膜原水槽10へ
排出される。更に洗浄を行うときは、再び洗浄液5′を
循環装置3により膜水槽1へ供給し循環水6を得る。以
上を繰り返して膜モジュール2の洗浄を終了する。バル
ブを膜原水槽10に切り換えて循環装置3を駆動するこ
とにより装置の運転を再開する。
That is, the circulating water 6 passes through the membrane water tank 1 many times and circulates for a while, and the dirty circulating water 6 is discharged to the membrane raw water tank 10 by switching a valve (not shown). It When further cleaning is performed, the cleaning liquid 5'is again supplied to the membrane water tank 1 by the circulation device 3 to obtain the circulating water 6. By repeating the above, the cleaning of the membrane module 2 is completed. By switching the valve to the membrane raw water tank 10 and driving the circulation device 3, the operation of the device is restarted.

【0020】(実施の第2形態)次に図2により本発明
による膜分離処理装置の実施の第2形態について説明す
る。図2において、内部に膜モジュール2を収納した膜
水槽1は膜原水槽8内に設けている。膜水槽1は下部に
流入口が設けられ、その流入口にポンプ等の循環装置3
が設けられている。また、膜水槽1の上部には開閉装置
7を設けた流出口があけられている。
(Second Embodiment) Next, a second embodiment of the membrane separation treatment apparatus according to the present invention will be described with reference to FIG. In FIG. 2, the membrane water tank 1 having the membrane module 2 accommodated therein is provided in the membrane raw water tank 8. The membrane water tank 1 is provided with an inflow port at the bottom, and a circulation device 3 such as a pump is provided at the inflow port.
Is provided. An outlet provided with an opening / closing device 7 is opened in the upper portion of the membrane water tank 1.

【0021】このように、図2の膜分離処理装置は、膜
水槽1を膜原水槽8内に設置した例である。このように
構成された図2の膜分離処理装置において、通常の運転
時は、開閉装置7を開とし循環装置3を駆動して運転
し、膜原水槽8内の膜原水を膜水槽1内に流通させ膜原
水から汚濁物質と分離した処理水4を取り出す。
As described above, the membrane separation treatment apparatus of FIG. 2 is an example in which the membrane water tank 1 is installed in the membrane raw water tank 8. In the membrane separation treatment apparatus of FIG. 2 configured in this way, during normal operation, the opening / closing device 7 is opened and the circulation device 3 is driven to drive the raw membrane water in the raw membrane water tank 8 into the membrane water tank 1. The treated water 4 separated from the pollutants is taken out from the raw membrane water.

【0022】一方、膜モジュールを膜原水以外の洗浄液
5′で洗浄する時は、開閉装置7を「閉」にして循環装
置3を逆回転させ洗浄液5′を膜水槽1に供給し、膜水
槽1内の液体が置換された時点で、循環装置3を停止
し、膜モジュール2の浸漬洗浄を行う。浸漬洗浄が終了
したら、開閉装置7を開とし循環装置3を駆動して通常
の運転を再開する。
On the other hand, when the membrane module is washed with the washing liquid 5'other than the raw membrane water, the opening / closing device 7 is closed and the circulation device 3 is rotated in the reverse direction to supply the washing liquid 5'to the membrane water tank 1 When the liquid in 1 is replaced, the circulation device 3 is stopped and the membrane module 2 is washed by immersion. When the immersion cleaning is completed, the opening / closing device 7 is opened and the circulation device 3 is driven to resume normal operation.

【0023】以上の実施の第1形態及び第2形態におい
て、洗浄により発生する汚泥分は、それぞれ膜原水槽8
及び10に残溜することになるが、膜原水槽8及び10
内の膜原水は循環装置(図示なし)により循環されてお
り、膜原水槽8及び10内の汚泥分は徐々に槽外へ抜き
出されるようになっている。
In the above-described first and second embodiments, the sludge components generated by washing are respectively the membrane raw water tank 8
And 10 will remain in the membrane raw water tanks 8 and 10.
The membrane raw water inside is circulated by a circulation device (not shown), and the sludge component in the membrane raw water tanks 8 and 10 is gradually drawn out of the tank.

【0024】[0024]

【発明の効果】以上説明したように、膜原水から汚濁物
質を分離する膜モジュールを用いた本発明による膜分離
処理装置においては、膜モジュールを内部に収納すると
共に内部に膜原水を流出入させるように構成した膜水槽
を、膜原水槽とは別に設けたもので、これによれば膜モ
ジュールの洗浄はこの膜水槽内で行えるので、不衛生作
業であった膜モジュールの取り出しや人手による洗浄等
を不要にするものである。
As described above, in the membrane separation treatment apparatus according to the present invention using the membrane module for separating pollutants from the membrane raw water, the membrane module is housed inside and the membrane raw water flows in and out. The membrane water tank configured as described above is provided separately from the membrane raw water tank. According to this, the membrane module can be cleaned in this membrane water tank. Etc. are unnecessary.

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

【図1】本発明の実施の第1形態に係る膜分離処理装置
の構成図。
FIG. 1 is a configuration diagram of a membrane separation processing apparatus according to a first embodiment of the present invention.

【図2】本発明の実施の第2形態に係る膜分離処理装置
の構成図。
FIG. 2 is a configuration diagram of a membrane separation processing apparatus according to a second embodiment of the present invention.

【図3】従来の膜分離処理装置を示す構成図。FIG. 3 is a configuration diagram showing a conventional membrane separation processing apparatus.

【符号の説明】[Explanation of symbols]

1 膜水槽 2 膜モジュール 3 循環装置 4 処理水 5 膜原水 5′ 洗浄液 6 循環水 7 開閉装置 8 膜原水槽 9 散気管 10 膜原水槽 1 Membrane water tank 2 Membrane module 3 Circulation device 4 Treated water 5 Membrane raw water 5'Cleaning liquid 6 Circulating water 7 Switchgear 8 Membrane raw water tank 9 Air diffuser 10 Membrane raw water tank

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 膜原水から汚濁物質を分離する膜モジュ
ールを用いた膜分離処理装置において、前記膜モジュー
ルを内部に収納すると共に内部に膜原水を流出入させる
ように構成した膜水槽を、曝気を行う膜原水槽とは別
に、設けたことを特徴とする膜分離処理装置。
1. A membrane separation treatment apparatus using a membrane module for separating pollutants from membrane raw water, wherein the membrane module is housed inside and a membrane water tank configured to let the membrane raw water flow in and out is aerated. A membrane separation treatment device, characterized in that it is provided separately from the membrane raw water tank.
【請求項2】 前記膜水槽内の膜原水を膜モジュール洗
浄用液体に置換可能に構成してなる請求項1に記載の膜
分離処理装置。
2. The membrane separation treatment apparatus according to claim 1, wherein the membrane raw water in the membrane water tank can be replaced with a membrane module cleaning liquid.
JP24928095A 1995-09-27 1995-09-27 Membrane separation processing equipment Expired - Lifetime JP3310836B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24928095A JP3310836B2 (en) 1995-09-27 1995-09-27 Membrane separation processing equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24928095A JP3310836B2 (en) 1995-09-27 1995-09-27 Membrane separation processing equipment

Publications (2)

Publication Number Publication Date
JPH0985065A true JPH0985065A (en) 1997-03-31
JP3310836B2 JP3310836B2 (en) 2002-08-05

Family

ID=17190621

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24928095A Expired - Lifetime JP3310836B2 (en) 1995-09-27 1995-09-27 Membrane separation processing equipment

Country Status (1)

Country Link
JP (1) JP3310836B2 (en)

Also Published As

Publication number Publication date
JP3310836B2 (en) 2002-08-05

Similar Documents

Publication Publication Date Title
JPH04131182A (en) Biological treating device for organic polluted water
US5997743A (en) Water treatment method using hollow fiber membrane and apparatus therefor
JPH0919694A (en) Ozone purifier
JP2003001293A (en) Method and apparatus for removing nitrogen in membrane separation type oxidation ditch
JPH0947598A (en) Washing machine
JPH0985065A (en) Membrane separation treatment apparatus
JPH08290045A (en) Immersion type membrane cartridge cleaning method
JP2005279495A (en) Immersion type membrane separator, method of cleaning a diffuser and membrane separation method
JPH10296238A (en) Pressure circulation filter
JPH11267396A (en) Washing machine
JPH0957075A (en) Membrane separation device
JP3695907B2 (en) Air supply device for septic tank
JPH08108017A (en) Circulating bath
JP3465381B2 (en) Filtration tank of bath water circulation purification device
JP2849555B2 (en) Hot water circulation treatment equipment
JP2007061705A (en) Septic tank
JP4248116B2 (en) Advanced membrane processing equipment
JPH09239247A (en) Immersion type membrane separation apparatus and membrane washing method therein
JP3715709B2 (en) Bathtub cleaning equipment
JPH10211489A (en) Purifying system
JP2002136979A (en) Sewage purification equipment
JP2002126459A (en) Internal pressure type membrane processing equipment
JPH11239788A (en) Bath water cleaning apparatus
JP3102385U (en) Waste liquid stirring device in grease trap
JPH0910786A (en) Wastewater treatment equipment

Legal Events

Date Code Title Description
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20020423

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090524

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090524

Year of fee payment: 7

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090524

Year of fee payment: 7

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313113

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090524

Year of fee payment: 7

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090524

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100524

Year of fee payment: 8

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100524

Year of fee payment: 8

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100524

Year of fee payment: 8

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110524

Year of fee payment: 9

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120524

Year of fee payment: 10

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130524

Year of fee payment: 11

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140524

Year of fee payment: 12

EXPY Cancellation because of completion of term