JPH0557161A - Method for regenerating hollow fiber filter medium - Google Patents

Method for regenerating hollow fiber filter medium

Info

Publication number
JPH0557161A
JPH0557161A JP22267991A JP22267991A JPH0557161A JP H0557161 A JPH0557161 A JP H0557161A JP 22267991 A JP22267991 A JP 22267991A JP 22267991 A JP22267991 A JP 22267991A JP H0557161 A JPH0557161 A JP H0557161A
Authority
JP
Japan
Prior art keywords
hollow fiber
fiber membrane
oil
alcohol
filter medium
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
JP22267991A
Other languages
Japanese (ja)
Inventor
Keijiro Yasumura
恵二朗 安村
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.)
Toshiba Corp
Original Assignee
Toshiba 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 Toshiba Corp filed Critical Toshiba Corp
Priority to JP22267991A priority Critical patent/JPH0557161A/en
Publication of JPH0557161A publication Critical patent/JPH0557161A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To improve cleaning effect by using a new cleaning composition in the regeneration of oil-polluted hollow fiber filter medium. CONSTITUTION:Hollow fiber filter medium polluted with deposited suspended substance is cleaned with the following cleaning composition (wt.%): ethanol 50-60, water 10-30, sodium metasilicate 5-10, potassium hydroxide 3-5, surfactant 1-2, xylene 0.1-0.5. Oil is saponified by sodium metasilicate and potassium hydroxide.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は懸濁物を含んだ原液を中
空糸膜製濾材で濾過して濾液とする中空糸膜濾過装置に
おいて、前記中空糸膜製濾材に付着した懸濁物を洗浄剤
で洗浄して濾過能力を再生する中空糸膜製濾材の再生方
法に関する。
BACKGROUND OF THE INVENTION The present invention relates to a hollow fiber membrane filtering apparatus for filtering a stock solution containing a suspension through a hollow fiber membrane filtering material to obtain a filtrate, and the suspension attached to the hollow fiber membrane filtering material. The present invention relates to a method for regenerating a hollow fiber membrane-made filter material that is washed with a detergent to regenerate the filtration ability.

【0002】[0002]

【従来の技術】原子力施設、特に原子力発電所では作業
員の使用した衣服の洗濯水や手洗い、シャワー等の廃水
および機械油等を含んだ放射性廃水が発生する。これら
の廃水は皮脂,タンパク質,バクテリア,鉱物油の有機
成分濃度が高いことが特長である。このような廃水は放
射能濃度が極めて低く、洗浄剤成分や糸屑,髪の毛,埃
等の浮遊性懸濁物を含み、かつ洗浄剤成分,シャンプー
等による化学的酸素量(COD)が高い。これらの廃水
を処理する場合、浮遊性懸濁物はストレーナ等により糸
屑等の大きなごみを除去し、中空糸膜濾過装置を通して
濾過した後、放射能を測定して規定濃度以下の放射能で
あることを確認して環境に放出している。なお、中空糸
膜濾過装置はタンク内に中空糸膜たとえば有機高分子化
合物の細長い糸状中空繊維を多数本束ねて濾材として組
込んでなるものである。
2. Description of the Related Art Nuclear power facilities, especially nuclear power plants, generate waste water for washing clothes used by workers, hand washing, showers and the like, and radioactive waste water containing machine oil and the like. These wastewaters are characterized by high concentrations of organic components in sebum, proteins, bacteria and mineral oils. Such wastewater has an extremely low radioactivity concentration, contains a floating suspension of detergent components, lint, hair, dust and the like, and has a high chemical oxygen content (COD) due to the detergent components, shampoo and the like. When treating these wastewaters, the floating suspension removes large debris such as lint with a strainer, etc., and after filtering through a hollow fiber membrane filtration device, the radioactivity is measured and radioactivity below the specified concentration is measured. Confirm that it is released into the environment. The hollow fiber membrane filtering device comprises a hollow fiber membrane, for example, a plurality of elongated filamentous hollow fibers of an organic polymer compound, which are bundled in a tank and incorporated as a filter medium.

【0003】[0003]

【発明が解決しようとする課題】水中の懸濁物を中空糸
膜を通して濾過する場合には濾過された粒子,油分等が
中空糸膜の表面に付着し、次第に濾過効率が低下する。
特に、油分等の粘着性のある物質が付着すると再生は非
常に困難である。このような場合に過酸化水素、または
アルコールおよびアルコールに微量溶解する水酸化カリ
ウムを溶解した洗浄剤で洗浄する方法が知られている。
When a suspension in water is filtered through a hollow fiber membrane, the filtered particles, oil, etc. adhere to the surface of the hollow fiber membrane, and the filtration efficiency gradually decreases.
In particular, if a sticky substance such as oil is attached, it is very difficult to regenerate it. In such a case, there is known a method of cleaning with hydrogen peroxide or a cleaning agent in which alcohol and a small amount of potassium hydroxide dissolved in alcohol are dissolved.

【0004】しかしながら、過酸化水素による洗浄は溶
解性がなく、酸化力で油分を分解しているので、その効
果が十分でなく、かつ中空糸膜の劣化の問題がある。ま
た、アルコールによる洗浄は過酸化水素と同様に洗浄効
果が十分でなく、火災等の問題がある。アルコールに微
量溶解する水酸化カリウムを添加する方法は洗浄効果は
多少改善されるが、水酸化カリウムがアルコールに多量
に溶解しないので洗浄力は大幅に増加しない課題があ
る。
However, washing with hydrogen peroxide is not soluble and decomposes oil components by oxidizing power, so that the effect is not sufficient and there is a problem of deterioration of the hollow fiber membrane. Further, cleaning with alcohol is not sufficient in cleaning effect like hydrogen peroxide, and there is a problem such as fire. The method of adding a small amount of potassium hydroxide that is soluble in alcohol improves the cleaning effect to some extent, but since potassium hydroxide does not dissolve in alcohol in a large amount, the cleaning power does not increase significantly.

【0005】本発明は上記課題を解決するためになされ
たもので、中空糸膜に付着した油分,バクテリア,浮遊
性懸濁物を効率的に洗浄して再生できるようにした中空
糸膜製濾材の再生方法を提供することにある。
The present invention has been made to solve the above-mentioned problems, and it is a hollow fiber membrane filter material capable of efficiently cleaning and regenerating oil, bacteria and floating suspensions attached to the hollow fiber membrane. Is to provide a method of reproducing.

【0006】[0006]

【課題を解決するための手段】本発明は、懸濁物を含ん
だ原液を中空糸膜製濾材を通して濾過し、油汚染した前
記中空糸膜製濾材を、重量%で、メチルアルコール,エ
チルアルコール,ブチルアルコールから選択された少な
くとも1種50〜60%,水10〜30%,メタケイ酸ナトリウ
ムまたはオルソケイ酸ナトリウムの少なくとも1種,水
酸化カリウム,水酸化ナトリウム,炭酸ナトリウムから
選択された少なくとも1種3〜5%,界面活性剤1〜2
%,キシレン,ベンゼン,トルエンから選択された少な
くとも1種 0.1〜 0.5%からなる洗浄剤で洗浄すること
を特徴とする。
According to the present invention, an undiluted solution containing a suspension is filtered through a hollow fiber membrane filter material, and the oil-contaminated hollow fiber membrane filter material is used in a weight percentage of methyl alcohol or ethyl alcohol. , At least one selected from butyl alcohol 50-60%, water 10-30%, at least one selected from sodium metasilicate or sodium orthosilicate, at least one selected from potassium hydroxide, sodium hydroxide and sodium carbonate 3-5%, surfactant 1-2
%, Xylene, benzene, toluene, and at least one selected from 0.1 to 0.5%.

【0007】[0007]

【作用】本発明で使用する洗浄剤の組成と成分割合の限
定理由は次のとおりである。 (1) メチルアルコール,エチルアルコール,ブチルアル
コールから選択される少なくとも1種:50〜60%
The reasons for limiting the composition and the component ratio of the detergent used in the present invention are as follows. (1) At least one selected from methyl alcohol, ethyl alcohol and butyl alcohol: 50-60%

【0008】上記アルコールは油分を除去するために使
用するもので、60%を超えると消防法による危険物の規
制を受けるので、大量に取扱う場合には燃焼の可能性が
あって危険であり、一方、50%未満では油分に対する洗
浄効果がうすらぎ望ましくない。なお、原子力発電所内
で使用している中空糸膜製濾材を洗浄するには洗浄剤は
約10〜30ton 必要であり、このような大量のアルコール
を純粋(〜 100%)で使用することは危険である。 (2) 水:10〜30%
The above alcohol is used to remove oil, and if it exceeds 60%, it is subject to the regulation of dangerous substances by the Fire Service Law, so if it is handled in large quantities, there is a possibility of burning and it is dangerous. On the other hand, if it is less than 50%, the cleaning effect on oil is thin and undesirable. About 10 to 30 tons of cleaning agent is required to clean the hollow fiber membrane filter media used in the nuclear power plant. It is dangerous to use such a large amount of alcohol in pure (~ 100%). Is. (2) Water: 10-30%

【0009】水はメタケイ酸ナトリウム,水酸化カリウ
ム,界面活性剤などの化合物を溶解するものであり、こ
れらの化合物はアルコールには溶解しない。水の量が10
〜30%からはずれるのは溶解度との関係で望ましくな
い。 (3) メタケイ酸ナトリウム,オルソケイ酸ナトリウムの
うち少なくとも1種:5〜10%
Water dissolves compounds such as sodium metasilicate, potassium hydroxide and a surfactant, and these compounds are not soluble in alcohol. The amount of water is 10
Departure from -30% is not desirable due to solubility. (3) At least one of sodium metasilicate and sodium orthosilicate: 5 to 10%

【0010】メタまたはオルソケイ酸ナトリウムはアル
コールまたは水中に油分を分散させるための分散剤であ
り、その必要量は水−アルコール系溶剤の溶解度から決
定されるもので、5〜10%からはずれるのは望ましくな
い。 (4) 水酸化カリウム,水酸化ナトリウム,炭酸ナトリウ
ムから選択される少なくとも1種:3〜5%
Sodium meta or orthosilicate is a dispersant for dispersing oil in alcohol or water, and its necessary amount is determined by the solubility of water-alcohol type solvent, and it may deviate from 5 to 10%. Not desirable. (4) At least one selected from potassium hydroxide, sodium hydroxide and sodium carbonate: 3 to 5%

【0011】これらは中空糸膜から油分を脱脂するため
のもので、水−アルコール系溶剤の溶解度からその量が
決まる。したがって、3〜5%からはずれるのは望まし
くない。 (5) 界面活性剤:1〜2%
These are for degreasing the oil content from the hollow fiber membrane, and the amount thereof is determined by the solubility of the water-alcohol solvent. Therefore, deviation from 3-5% is not desirable. (5) Surfactant: 1-2%

【0012】界面活性剤としては陰イオン界面活性剤に
たとえばドデシルベンゼンスルホン酸ナトリウムが、非
イオン界面活性剤にたとえばノニルフェニール・ポリオ
キシエチレン・エーテルが使用される。これらは2種類
を使用しても効果は同等である。
As the surfactant, for example, sodium dodecylbenzenesulfonate is used as the anionic surfactant, and nonylphenyl polyoxyethylene ether is used as the nonionic surfactant. Even if two types are used, the effects are the same.

【0013】界面活性剤の量が1〜2%において、ミセ
ル(両親媒分質が親水基,親油基を内に向けて油分を溶
かし込む)を形成するが、1〜2%から外れるのは望ま
しくない。 (6) キシレン,ベンゼン,トルエンから選択される少な
くとも1種:0.1〜 0.5% これらは油分を溶解させるために必要で、その量は水に
対する溶解度から決まり、 0.1〜 0.5%の範囲内からは
ずれるのは望ましくない。
When the amount of the surfactant is 1 to 2%, micelles are formed (the amphipathic substance dissolves the oil with the hydrophilic group and the lipophilic group facing inward), but the amount is out of the range of 1 to 2%. Is not desirable. (6) At least one selected from xylene, benzene, and toluene: 0.1 to 0.5% These are necessary to dissolve the oil component, and the amount is determined by the solubility in water, and it is out of the range of 0.1 to 0.5%. Is not desirable.

【0014】[0014]

【実施例】図1を参照しながら本発明に係る中空糸膜製
濾材の再生方法の一実施例を説明する。
EXAMPLE An example of a method for recycling a hollow fiber membrane-made filter material according to the present invention will be described with reference to FIG.

【0015】図1は本実施例の効果を確認するための試
験装置の系統図を示している。図中符号1は原液2を貯
留した原液タンクで、この原液タンク1には中空糸膜製
濾材3を内蔵した濾過装置4に原液2を送り込むための
給液管5が接続されている。給液管5には給液ポンプ
6、第1の弁7および第1の圧力計8が順次接続されて
いる。濾過装置4の上端には濾液流出管9が接続されて
いる。この濾液流出管9には第2の圧力計10、第2の弁
11、流量調整弁12、流量計13、温度計14および積算流量
計15が順次接続されている。濾過装置4の側面には洗浄
剤タンク16が第3の弁17を介して洗浄剤給送管18により
接続されている。濾過装置4の下端には空気供給源19が
第4の弁20を介しバブリングガス供給管21により接続さ
れている。また、濾過装置4の下端には洗浄液流出管23
が接続されており、この洗浄液流出管23には給液管5の
他端が接続している。洗浄液流出管23は第5の弁22を介
して洗浄液受タンク24に接続されている。上記試験装置
において、原液2を表1に示した組成に模擬して原液タ
ンク1内に貯留する。
FIG. 1 shows a system diagram of a test apparatus for confirming the effect of this embodiment. In the figure, reference numeral 1 is a stock solution tank storing a stock solution 2, and a solution supply pipe 5 for feeding the stock solution 2 to a filtration device 4 having a hollow fiber membrane-made filter material 3 incorporated therein is connected to the stock solution tank 1. A liquid supply pump 6, a first valve 7 and a first pressure gauge 8 are sequentially connected to the liquid supply pipe 5. A filtrate outflow pipe 9 is connected to the upper end of the filtration device 4. The filtrate outlet pipe 9 has a second pressure gauge 10 and a second valve.
11, a flow rate adjusting valve 12, a flow meter 13, a thermometer 14 and an integrating flow meter 15 are sequentially connected. A cleaning agent tank 16 is connected to a side surface of the filtering device 4 via a third valve 17 by a cleaning agent feeding pipe 18. An air supply source 19 is connected to the lower end of the filtering device 4 by a bubbling gas supply pipe 21 via a fourth valve 20. In addition, at the lower end of the filtration device 4, the cleaning liquid outflow pipe 23
Is connected, and the other end of the liquid supply pipe 5 is connected to the cleaning liquid outflow pipe 23. The cleaning liquid outflow pipe 23 is connected to the cleaning liquid receiving tank 24 via the fifth valve 22. In the test apparatus, the stock solution 2 is simulated in the composition shown in Table 1 and stored in the stock solution tank 1.

【0016】[0016]

【表1】 [Table 1]

【0017】また、洗浄剤タンク16内に、重量%で、エ
チルアルコール60%,水22.5%,メタケイ酸ナトリウム
10%,水酸化カリウム5%,界面活性剤2%およびキシ
レン0.5%からなる洗浄剤を充填する。
Further, in the cleaning agent tank 16, in weight%, ethyl alcohol 60%, water 22.5%, sodium metasilicate
Fill a detergent consisting of 10%, potassium hydroxide 5%, surfactant 2% and xylene 0.5%.

【0018】ここで、第1および第2の弁7,11と流量
調整弁12を開とし、第3,第4および第5の弁17,20,
22を閉じる。給液ポンプ6を駆動し、流量計13の指示に
より所定流量に設定し、原液2を連続して濾過装置4内
に供給する。この時、濾過装置4の入口圧力を第1の圧
力計8で、出口圧力を第2の圧力計10で測定し、規定圧
力に到達した時点で給液ポンプ6を停止する。第1の弁
7と第2の弁11を閉じる。そして、洗浄剤タンク16から
第3の弁17を開き、洗浄剤を濾過装置4内に流入する。
この時、第4の弁20を開き空気供給源19から空気を濾過
装置4内に吹き込んでバブリングを行う。所定の時間経
過後、第5の弁22を開いて洗浄液を洗浄液流出管23を通
して洗浄液受タンク24内に貯蔵する。この洗浄操作によ
り中空糸膜製濾材3を再生する。そして、再び表1に模
擬した原液2を濾過装置4に供給し中空糸膜製濾材3で
濾過操作を行う。このようにして、濾過操作後の中空糸
膜製濾材3の洗浄操作を行った結果を表2に示す。
Here, the first and second valves 7, 11 and the flow rate adjusting valve 12 are opened, and the third, fourth and fifth valves 17, 20,
Close 22. The liquid supply pump 6 is driven, a predetermined flow rate is set according to an instruction from the flow meter 13, and the stock solution 2 is continuously supplied into the filtration device 4. At this time, the inlet pressure of the filtration device 4 is measured by the first pressure gauge 8 and the outlet pressure thereof is measured by the second pressure gauge 10. When the specified pressure is reached, the liquid supply pump 6 is stopped. The first valve 7 and the second valve 11 are closed. Then, the third valve 17 is opened from the cleaning agent tank 16 to allow the cleaning agent to flow into the filtering device 4.
At this time, the fourth valve 20 is opened and air is blown into the filter device 4 from the air supply source 19 to perform bubbling. After a lapse of a predetermined time, the fifth valve 22 is opened and the cleaning liquid is stored in the cleaning liquid receiving tank 24 through the cleaning liquid outflow pipe 23. The hollow fiber membrane filter material 3 is regenerated by this washing operation. Then, the stock solution 2 simulated in Table 1 is supplied again to the filtration device 4, and the hollow fiber membrane-made filter material 3 is used for the filtration operation. The results of the washing operation of the hollow fiber membrane-made filter material 3 after the filtration operation are shown in Table 2.

【0019】[0019]

【表2】 [Table 2]

【0020】表2から明らかなように本実施例によれば
油分,バクテリア,浮遊性懸濁物により差圧が高くなっ
た中空糸膜製濾材は上記組成の洗浄剤により洗浄され
て、初期の差圧に回復したことが認められる。
As is apparent from Table 2, according to the present example, the hollow fiber membrane filter material having a high differential pressure due to oil, bacteria and floating suspension was washed with the detergent having the above composition, and It is recognized that the differential pressure has been restored.

【0021】[0021]

【発明の効果】本発明によれば、油汚染した中空糸膜製
濾材をアルコール,水,メタケイ酸ナトリウム,水酸化
カリウム等を主成分とした洗浄剤で鹸化反応によって洗
浄し、効率的に再生することができる。
EFFECTS OF THE INVENTION According to the present invention, an oil-contaminated filter material made of hollow fiber membrane is efficiently regenerated by washing it with a detergent containing alcohol, water, sodium metasilicate, potassium hydroxide or the like as a main component by a saponification reaction. can do.

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

【図1】本発明に係る中空糸膜製濾材の再生方法の一実
施例における洗浄剤の効果を確認するための試験装置を
示す系統図。
FIG. 1 is a system diagram showing a test device for confirming the effect of a cleaning agent in an example of a method for recycling a hollow fiber membrane-made filter material according to the present invention.

【符号の説明】[Explanation of symbols]

1…原液タンク、2…原液、3…中空糸膜製濾材、4…
濾過装置、5…給液管、6…給液ポンプ、7…第1の
弁、8…第1の圧力計、9…濾液流出管、10…第2の圧
力計、11…第2の弁、12…流量調節弁、13…流量計、14
…温度計、15…積算流量計、16…洗浄剤タンク、17…第
3の弁、18…洗浄剤給送管、19…空気供給源、20…第4
の弁、21…バブリングガス供給管、22…第5の弁、23…
洗浄液流出管、24…洗浄液受タンク。
1 ... Stock solution tank, 2 ... Stock solution, 3 ... Hollow fiber membrane filter material, 4 ...
Filtration device, 5 ... Liquid supply pipe, 6 ... Liquid supply pump, 7 ... First valve, 8 ... First pressure gauge, 9 ... Filtrate outflow pipe, 10 ... Second pressure gauge, 11 ... Second valve , 12 ... Flow control valve, 13 ... Flow meter, 14
... thermometer, 15 ... integrated flow meter, 16 ... detergent tank, 17 ... third valve, 18 ... detergent supply pipe, 19 ... air supply source, 20 ... fourth
Valve, 21 ... Bubbling gas supply pipe, 22 ... Fifth valve, 23 ...
Cleaning solution outflow pipe, 24 ... Cleaning solution receiving tank.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 懸濁物を含んだ原液を中空糸膜製濾材を
通して濾過し、油汚染した前記中空糸膜製濾材を、重量
%で、メチルアルコール,エチルアルコール,ブチルア
ルコールから選択された少なくとも1種50〜60%,水10
〜30%,メタケイ酸ナトリウムまたはオルソケイ酸ナト
リウムの少なくとも1種,水酸化カリウム,水酸化ナト
リウム,炭酸ナトリウムから選択された少なくとも1種
3〜5%,界面活性剤1〜2%,キシレン,ベンゼン,
トルエンから選択された少なくとも1種 0.1〜 0.5%か
らなる洗浄剤で洗浄することを特徴とする中空糸膜製濾
材の再生方法。
1. An undiluted solution containing a suspension is filtered through a hollow fiber membrane filter material, and the oil-contaminated hollow fiber membrane filter material is at least selected from methyl alcohol, ethyl alcohol and butyl alcohol in weight%. 50-60% of one kind, water 10
-30%, at least one of sodium metasilicate or sodium orthosilicate, at least one selected from potassium hydroxide, sodium hydroxide, sodium carbonate 3-5%, surfactant 1-2%, xylene, benzene,
A method for regenerating a hollow fiber membrane-made filter medium, which comprises washing with a detergent comprising 0.1 to 0.5% of at least one selected from toluene.
JP22267991A 1991-09-03 1991-09-03 Method for regenerating hollow fiber filter medium Pending JPH0557161A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22267991A JPH0557161A (en) 1991-09-03 1991-09-03 Method for regenerating hollow fiber filter medium

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22267991A JPH0557161A (en) 1991-09-03 1991-09-03 Method for regenerating hollow fiber filter medium

Publications (1)

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JPH0557161A true JPH0557161A (en) 1993-03-09

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JP22267991A Pending JPH0557161A (en) 1991-09-03 1991-09-03 Method for regenerating hollow fiber filter medium

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1304157A1 (en) * 2001-10-19 2003-04-23 Technologies Avancees & Membranes Industrielles S.A. Method for cleaning a ceramic membrane for use in the filtration of wines
CN112915802A (en) * 2021-02-05 2021-06-08 国家能源集团国源电力有限公司 Alkali washing agent and alkali washing method for reverse osmosis device in coal-fired boiler water supply system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1304157A1 (en) * 2001-10-19 2003-04-23 Technologies Avancees & Membranes Industrielles S.A. Method for cleaning a ceramic membrane for use in the filtration of wines
FR2831078A1 (en) * 2001-10-19 2003-04-25 Tech Avancees & Membranes Ind NEW PROCESS FOR CLEANING A CERAMIC MEMBRANE USED IN WINE FILTRATION
CN112915802A (en) * 2021-02-05 2021-06-08 国家能源集团国源电力有限公司 Alkali washing agent and alkali washing method for reverse osmosis device in coal-fired boiler water supply system

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