JP2004154694A - Solid-liquid separating method using centrifugal separator - Google Patents

Solid-liquid separating method using centrifugal separator Download PDF

Info

Publication number
JP2004154694A
JP2004154694A JP2002323317A JP2002323317A JP2004154694A JP 2004154694 A JP2004154694 A JP 2004154694A JP 2002323317 A JP2002323317 A JP 2002323317A JP 2002323317 A JP2002323317 A JP 2002323317A JP 2004154694 A JP2004154694 A JP 2004154694A
Authority
JP
Japan
Prior art keywords
liquid
solid
rotating body
treated
separated
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
JP2002323317A
Other languages
Japanese (ja)
Other versions
JP4047136B2 (en
Inventor
Masatake Noguchi
正剛 野口
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 Kakoki Kaisha Ltd
Original Assignee
Mitsubishi Kakoki Kaisha 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 Kakoki Kaisha Ltd filed Critical Mitsubishi Kakoki Kaisha Ltd
Priority to JP2002323317A priority Critical patent/JP4047136B2/en
Publication of JP2004154694A publication Critical patent/JP2004154694A/en
Application granted granted Critical
Publication of JP4047136B2 publication Critical patent/JP4047136B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Centrifugal Separators (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a solid-liquid separating method using a centrifugal separator by which the liquid to be treated can be separated into a liquid and a solid without hindrance, and from which the separated liquid and solid can be discharged easily and then the separated solid can be sorted even when the liquid to be treated contains voluminus solid and the solid apt to stick or to break. <P>SOLUTION: The centrifugal separator is constituted so that the solid-mixed liquid to be treated is supplied to the inside of a rotating body and separated into the liquid and the solid by the centrifugal force and at least the separated liquid is discharged continuously. A fixed amount of a viscous substance which is hardly dissolved in the liquid to be treated and has fluidity is supplied to the inside of the rotating body as a solid capturing agent all at once or continuously. The liquid to be treated is supplied continuously and separated into the liquid and the solid by the centrifugal force. Only the separated liquid or all of the separated liquid and the separated solid are discharged continuously, and the supply of the liquid to be treated is stopped and the contents in the rotating body is discharged after the prescribed time passes. <P>COPYRIGHT: (C)2004,JPO

Description

【0001】
【発明の属する技術分野】
本発明は、固形物が混入する被処理液を高速回転する回転体内に供給して遠心力で固液分離し、少なくとも分離した液体を連続的に排出する遠心分離機による固液分離方法に関するものである。
【0002】
【従来の技術】
従来、固形物や水分などを含有する潤滑油や燃料油などから、それらの固形物や水分などを分離除去して清浄油を回収したり、有用な固形物を含有する各種液体から固形物を分離して回収する固液分離などに、高速で回転する回転体の高い遠心力による比重差で固形物を分離する遠心分離機が使用されている。
【0003】
また、前記遠心分離機の中でも、回転体内に多数の分離板を積層した分離板群を装着し、分離板群の大きい沈降面積を利用して微粒子などを効率よく分離することができる分離板型遠心分離機が多くの産業分野で利用されており、特に船舶における潤滑油や燃料油の清浄化には一般的に多数使用されている。
【0004】
従来の遠心分離機について、分離板型遠心分離機を例として図2に基づいて説明すると、分離板型遠心分離機は、外周部にスラッジ排出孔13を有する回転胴11と回転胴11上部を覆蓋する回転体蓋部12から主になる回転体10を回転軸22に固定し、回転体10内に、截頭円錐形状の薄板からなる分離板14が回転体の軸方向に多数積層して形成された分離板群15およびスラッジ排出孔13を開閉する弁シリンダ16を装着している。
【0005】
前記遠心分離機による分離操作は、回転体10の軸心位置に挿入されて装着された原液供給管17の原液入口28から原液を供給し、供給された原液は、案内筒20を下降して回転体10の分離室内に導入され、回転軸22を介して回転される回転体10の高速回転による遠心力で、比重の軽い軽液と比重の重い重液や固形物を比重差で分離する。
【0006】
分離された重液や固形物は、回転体10内の最大径部に蓄積され、軽液は分離板群15の間隙を上向流通して軽液排出流路に具備された軽液排出インペラ18により汲み出されて、軽液出口26から回転体10外に排出される。また、前記の軽液の分離排出においては、軽液が分離板群15の間隙を上向流通する間に、残存する重液や固形物が更に沈降分離されるため、効率的に清澄化が促進されることになる。
【0007】
また、回転体10の最大径部に蓄積された重液および固形物の内の重液は、一定量蓄積すると重液案内板21と回転体蓋12内壁とで形成された重液流路を経て、重液インペラ19により汲み出されて、重液出口27から回転体10外に排出される。
【0008】
なお、前記軽液及び重液の排出は、回転体10に内設された調節板25により、液蓄積位置を調節することによって、制御される。
【0009】
また、給水装置24から所定の時間間隔で水を供給することにより、パイロットバルブ23の作動及び停止を制御し、それにより、内設された弁シリンダ16を上下に摺動させ、最大径部に具備されたスラッジ排出孔13を開閉制御することにより、回転体10の最大径部に蓄積された固形物と一部の重液からなるスラッジの排出が制御される。(例えば、特許文献1参照。)。
【0010】
また、前記分離板型遠心分離機には、重液排出インペラや調節板を設けずに、重液を排出する構造やノズル式スラッジ排出孔から連続的にスラッジを排出する構造又は弁シリンダ式スラッジ排出とノズル式スラッジ排出とを併用した装置も一般的に知られている(例えば、特許文献2参照。)。
【0011】
なお、本発明は、前記分離板型遠心分離機のみに適用されるものではなく、固形物が混入する被処理液を回転体内に供給して遠心力で固液分離し、少なくとも分離した液体を連続的に排出する遠心分離機であれば、無孔バスケット型遠心分離機なども適用が可能である。
【0012】
【特許文献1】
特公昭57−034023号公報
【特許文献2】
特開2001−239184号公報
【0013】
【発明が解決しようとする課題】
前記従来の遠心分離機における固液分離方法では、軽液、重液および固形物の分離が効率的に行われ、清澄度の高い軽液を容易に得ることができるが、スラッジ量が多くなると、弁開閉式スラッジ排出構造では、スラッジを排出する弁シリンダの開閉回数が多くななるため、弁シリンダや弁パッキンなどの摩耗が激しくなり、部品交換による経費や運転時間ロスが大きくなる問題がある。また、ノズル式スラッジ排出構造では、ノズル部でのスラッジの蓄積などによる排出不良を起す恐れもある。特に、固着しやすい固形物を含有する被処理液では、固形物が回転体の内壁に固着するため、排出が不可能となる問題があり、また、従来の遠心分離方法では、固形物の大きさや比重による分級操作は不可能である。
【0014】
本発明は、前記の問題に鑑みてなされたものであり、固形物が多く混入する被処理液、固着しやすい固形物を混入する被処理液又は破壊されやすい固形物を混入する被処理液であっても、支障なく分離して容易に排出でき、更に、固形物の分級も行うことができる遠心分離機による固液分離方法を提供する目的で成されたものである。
【0015】
【課題を解決するための手段】
前記目的を達成するための本発明の要旨は、請求項1に記載の発明においては、固形物が混入する被処理液を回転体内に供給して遠心力で固液分離し、少なくとも分離した液体を連続的に排出する遠心分離機において、被処理液に溶解しにくく且つ流動性を持つ粘稠性物質を固形物捕捉剤として回転体内に一定量供給したのち、被処理液を連続供給して遠心力で固液分離し、分離した液体を連続的に排出し、所定時間後に被処理液の供給を停止して回転体内容物を排出することを特徴とする遠心分離機による固液分離方法である。
【0016】
前記の構成により、分離固形物を被処理液に溶解しにくく且つ流動性を持つ粘稠性物質を固形物捕捉剤内に捕捉して保持し、その後に排出することにより、固形物が回転体の内壁に固着して、排出が不可能となる問題を生じる恐れがないため、固形物が多く混入する被処理液、固着しやすい固形物を混入する被処理液又は破壊されやすい固形物を混入する被処理液であっても、支障なく分離して容易に排出することができる。また、固形物に合わせて固形物捕捉剤の粘度や比重を適宜に調整することにより、固形物捕捉剤における固形物の沈降速度差で分級操作が可能となる。
【0017】
また、請求項2に記載の発明においては、固形物が混入する被処理液を回転体内に供給して遠心力で固液分離し、少なくとも分離した液体を連続的に排出する遠心分離機において、被処理液に溶解しにくく且つ流動性を持つ粘稠性物質を固形物捕捉剤として回転体内に連続供給しながら、被処理液を連続供給して遠心力で固液分離し、分離した液体と固形物捕捉剤とを連続的に排出することを特徴とする遠心分離機による固液分離方法である。
【0018】
前記の構成により、分離固形物を被処理液に溶解しにくく且つ流動性を持つ粘稠性物質を固形物捕捉剤内に捕捉して保持して連続的に排出することにより、固形物が回転体の内壁に固着して、排出が不可能となる問題を生じる恐れがないため、固形物が多く混入する被処理液、固着しやすい固形物を混入する被処理液又は破壊されやすい固形物を混入する被処理液であっても、支障なく分離して容易に排出することができる。また、固形物に合わせて固形物捕捉剤の粘度や比重を適宜に調整することにより、固形物捕捉剤における固形物の沈降速度差で分級操作が可能となる。
【0019】
また、請求項3に記載の発明においては、請求項1又は請求項2に記載の遠心分離機による固液分離方法において、遠心分離機が、回転体内に截頭円錐形状の薄板からなる分離板が軸方向に多数積層して内設した分離板型遠心分離機である遠心分離機による固液分離方法である。
【0020】
前記の構成により、請求項1における前記効果の他に、軽液が分離板の間隙を上向流通する間に、残存する重液や固形物が更に沈降分離され、効率的に清澄化が促進されるため、軽液、重液および固形物の分離が効率的に行われ、清澄度の高い軽液を容易に得ることができる。
【0021】
また、請求項4に記載の発明においては、請求項1、請求項2又は請求項3に記載の遠心分離機による固液分離方法において、被処理液が固形物が混入した油であり、固形物捕捉剤が高分子凝集剤を水で溶解して所定濃度に調整した粘稠性物質であり、分離した液体が清澄油である遠心分離機による固液分離方法である。
【0022】
前記の構成により、請求項1、請求項2又は請求項3における前記効果を最大限に発揮することができる。
【0023】
前記において、固形物捕捉剤としては、ヤマイモ分離エキス、ゼラチン、生物産生粘性物質、アルギン酸塩、寒天、ゼラチンなどの天然高分子物質、ポリビニルアルコール、ポリアクリル酸、ポリアクリルアミドなどの合成高分子物質、その他にアニオン高分子凝集剤、カチオン高分子凝集剤又はノニオン高分子凝集剤など水処理において使用される各種の凝集剤が使用でき、それらを水などの適宜溶剤で溶解し、被処理液の種類及び被処理液中の固形物の種類により適宜に濃度を調整し、ゲル状物質、ゾル状物質又は高粘度物質の粘稠性物質として用いられる。
【0024】
また、固形物捕捉剤を粘度で調整すると、10,000〜200,000cps、好ましくは、25,000〜150,000cpsを示す粘稠性物質を用いるのが好ましく、その比重は1.0〜1.1程度が好ましいが、本発明は、被処理液に溶解しにくく且つ流動性を持つ粘稠性物質であればよく、それらには限定されない。
【0025】
また、本分離方法において対象とする固形物が混入する被処理液としては、無機固形物を0.1〜2.0wt%含有する燃料油、廃鉱物油及び使用済食用油などの油脂、プランクトンなどの微生物を含有する水、複数の比重差を持つ固形物を含有して分級する必要のある油脂又は水などに適用することができる。
【0026】
【発明の実施の形態】
本発明の実施の形態を図面に基づいて説明する。図1は本発明の一実施の形態の遠心分離機の回転体部を拡大断面図として示した固液分離装置の系統図、図2は従来の遠心分離機の回転体部の拡大断面図である。なお、図1における符番において、回転体の各部においては図2と同一の番号を付した。
【0027】
図1において、符番1は、図示しないケーシング内に、外周部にスラッジ排出孔13を有する回転胴11と回転胴11上部を覆蓋する回転体蓋部12から主になる回転体10を回転軸22に固定し、回転体10内に、截頭円錐形状の薄板からなる分離板14が回転体の軸方向に多数積層して形成された分離板群15およびスラッジ排出孔13を開閉する弁シリンダ16を装着している分離板型遠心分離機である。
【0028】
また、前記分離板型遠心分離機1は、回転体10の軸心位置に原液供給管17が挿入されて装着され、供給される原液を回転体10の分離室内に導入する案内筒20が原液供給管17と同心的に設けられ、分離板群15の間隙を上向流通した軽液を排出する軽液排出流路に具備される軽液排出インペラ18と、回転体10の最大径部に蓄積された重液および固形物の内の重液を排出する重液案内板21と回転体蓋12内壁とで形成された重液流路を経て、重液排出流路に具備される重液インペラ19と、軽液及び重液の排出を調整する調節板25が内設されている。
【0029】
また、内設された弁シリンダ16を上下に摺動させ、最大径部に具備されたスラッジ排出孔13を開閉制御するための、作動水の給水装置24およびパイロットバルブ23が設けられている。
【0030】
符番2は、固形物が混入する被処理液(以下原液という)を貯留する原液槽、符番3は、遠心分離機1で固形物が分離され、清澄化された処理液を貯留する清澄液槽、符番4は、被処理液に溶解しにくく且つ流動性を持つゲル状物質、ゾル状物質又は高粘度物質の内の少なくとも1つの固形物捕捉剤を貯留する固形物捕捉剤槽である。
【0031】
また、符番5は、原液を原液槽2から遠心分離機1に供給する原液供給ポンプ、符番6は、固形物捕捉剤を固形物捕捉剤槽4から遠心分離機1に供給する固形物捕捉剤供給ポンプである。
【0032】
前記固液分離装置により、例えば、固形物が混入する油脂を原液とし、高分子凝集剤を水で溶解して所定粘度や比重に調整した高粘度物質を固形物捕捉剤として処理する方法について、以下詳述する。
【0033】
遠心分離機1を稼動したのち、固形物捕捉剤槽4で高分子凝集剤を水で溶解して所定比重の濃度に調整し、調整したゲル状の流動物(以下捕捉物質という。)を固形物捕捉剤供給ポンプ6で固形物捕捉剤供給経路bを経て、回転体10の軸心位置に挿入されて装着された原液供給管17の原液入口28から回転体10内に供給すると、捕捉物質は回転体10の最大径部に一定量蓄積されたのち、重液案内板21と回転体蓋12内壁とで形成された重液流路を経て、重液インペラ19により汲み出され、固形物捕捉剤循環経路dから固形物捕捉剤槽4に循環される。
【0034】
前記流動物の循環を継続しながら、原液槽2より原液を原液供給ポンプで原液供給経路aを経て回転体10の軸心位置に挿入されて装着された原液供給管17の原液入口28から供給し、供給された原液は、案内筒20を下降して回転体10の分離室内に導入され、回転軸を介して回転される回転体10の高速回転による遠心力で、比重の軽い油脂(以下軽液という)と比重の重い固形物および水と固形物の混合物(以下重液という)が比重差で分離される。
【0035】
分離された重液や固形物は、回転体10内の最大径部に蓄積され、軽液は分離板群15の間隙を上向流通して軽液排出流路に具備された軽液排出インペラ18により汲み出されて、軽液出口26から回転体10外に排出され、軽液排出流路cを経て清澄液槽3に貯留される。
【0036】
なお、前記の軽液の分離排出においては、軽液が分離板群15の間隙を上向流通する間に、残存する重液や固形物が更に沈降分離されるため、効率的に清澄化が促進されることになる。
【0037】
また、回転体10の最大径部に蓄積された重液および固形物の内の重液は、一定量蓄積すると重液案内板21と回転体蓋12内壁とで形成された重液流路を経て、重液インペラ19により汲み出されて、重液出口27から回転体10外に排出される。
【0038】
なお、前記軽液及び重液の排出は、回転体10に内設された調節板25により、重液蓄積位置を調節することによって、制御される。
【0039】
また、給水装置24から所定の時間間隔で水を供給することにより、パイロットバルブ23の作動及び停止を制御し、それにより、内設された弁シリンダ16を上下に摺動させ、最大径部に具備されたスラッジ排出孔13を開閉制御することにより、回転体10の最大径部に蓄積された固形物と一部の重液からなるスラッジの排出が制御されるが、殆どの固形物は流動物に捕捉されて排出されるため、殆どスラッジ排出孔13を開閉操作する必要がないか、少なくとも従来の方法と比較して、そのスラッジ排出孔13の開閉頻度は少なくなる。
【0040】
また、固形物に合わせて固形物捕捉剤の粘度や比重を適宜に調整することにより、固形物捕捉剤における固形物の沈降速度差で分級操作が可能である。
【0041】
【実施例】
次に本発明の方法により固形物濃度を調整したタービン油を処理した実施例について説明する。
タービン油32番に関東ローム11番を固形物濃度0.3kg/m3に調整したものを原液とした。また、固形物捕捉剤として、アニオン高分子凝集剤を水で溶解して2wt%濃度に調整した高粘度物質を用いた。
試験方法は、分離板型遠心分離機の回転体を、11,150Gの遠心力で回転させ、固形物捕捉剤を固形物捕捉剤供給ポンプにより2L/Hrで、原液供給管に接続した固形物捕捉剤供給管を介して回転体内に供給し、重液排出管を介して排出し循環した。被処理液は100L/Hrで原液供給管から供給した。
【0042】
前記の試験により、極めて回転体内壁に固着しやすい関東ロームが、固形物捕捉剤中に分散捕捉され、回転体壁面に固着することなく排出され、また、軽液として清澄なタービン油を得ることができ、長時間連続運転が可能であった。
【0043】
また、前記試験終了後、回転体内の固形物捕捉剤、タービン油及び関東ロームの混在する液を全量回収し、回分式遠心沈降管で1,000Gの遠心力により分離した結果、清澄なタービン油と関東ロームを分散混合した固形物捕捉剤に分離し、関東ロームの沈降はなかった。この結果、固形物が固形物捕捉剤に捕捉され、安定的に分散されていることが判明した。また、固形物捕捉剤を長時間循環使用することにも問題ないことが判明した。
【0044】
【発明の効果】
本発明は固形物が多く混入する被処理液、固着しやすい固形物を混入する被処理液又は破壊されやすい固形物を混入する被処理液であっても、支障なく分離して容易に排出でき、更に、固形物の分級も行うことができる遠心分離機による固液分離方法である。
【図面の簡単な説明】
【図1】本発明の一実施の形態の遠心分離機の回転体部を拡大断面図として示した固液分離装置の系統図
【図2】従来の遠心分離機の回転体部の拡大断面図
【符号の説明】
1:分離板型遠心分離機
2:原液槽
3:清澄液槽
4:固形物捕捉剤槽
5:原液供給ポンプ
6:固形物捕捉剤供給ポンプ
10:回転体
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a solid-liquid separation method using a centrifugal separator that supplies a liquid to be treated mixed with solids into a rotating body that rotates at a high speed, performs solid-liquid separation by centrifugal force, and continuously discharges at least the separated liquid. It is.
[0002]
[Prior art]
Conventionally, lubricating oils and fuel oils containing solids and water, etc. are separated and removed to remove the solids and water etc. to recover clean oil, or solids are collected from various liquids containing useful solids. 2. Description of the Related Art A centrifuge that separates solids with a specific gravity difference due to a high centrifugal force of a rotating body that rotates at a high speed is used for solid-liquid separation and the like that are separated and collected.
[0003]
Also, among the centrifugal separators, a separation plate group in which a separation plate group in which a number of separation plates are stacked in a rotating body is mounted, and fine particles and the like can be efficiently separated by utilizing a large settling area of the separation plate group. 2. Description of the Related Art Centrifuges are used in many industrial fields, and are generally used in large numbers for cleaning lubricating oil and fuel oil, particularly in ships.
[0004]
A conventional centrifugal separator will be described with reference to FIG. 2 using a separator plate type centrifuge as an example. The separator plate type centrifugal separator has a rotating drum 11 having a sludge discharge hole 13 on an outer peripheral portion and an upper portion of the rotating drum 11. The rotating body 10 mainly composed of the rotating body lid portion 12 to be covered is fixed to the rotating shaft 22, and a large number of separation plates 14 formed of frustoconical thin plates are laminated in the rotating body 10 in the axial direction of the rotating body. A valve cylinder 16 for opening and closing the formed separation plate group 15 and the sludge discharge hole 13 is mounted.
[0005]
In the separation operation by the centrifugal separator, the undiluted solution is supplied from the undiluted solution inlet 28 of the undiluted solution supply pipe 17 inserted and mounted at the axial position of the rotating body 10, and the supplied undiluted solution descends through the guide cylinder 20. The centrifugal force caused by the high speed rotation of the rotating body 10 introduced into the separation chamber of the rotating body 10 and rotated via the rotating shaft 22 separates the light liquid having a low specific gravity from the heavy liquid or the solid having a high specific gravity with a specific gravity difference. .
[0006]
The separated heavy liquid and solid matter are accumulated in the largest diameter portion in the rotating body 10, and the light liquid flows upward through the gap between the separation plate group 15 and the light liquid discharge impeller provided in the light liquid discharge passage. It is pumped out by 18 and discharged out of the rotating body 10 from the light liquid outlet 26. In the separation and discharge of the light liquid, the remaining heavy liquid and solids are further settled and separated while the light liquid flows upward through the gap between the separation plate groups 15, so that the clarification is efficiently performed. Will be promoted.
[0007]
When a certain amount of heavy liquid and solid liquid accumulated in the maximum diameter portion of the rotating body 10 accumulate, a heavy liquid flow path formed by the heavy liquid guide plate 21 and the inner wall of the rotating body lid 12 is formed. Then, it is pumped out by the heavy liquid impeller 19 and discharged out of the rotating body 10 from the heavy liquid outlet 27.
[0008]
The discharge of the light liquid and the heavy liquid is controlled by adjusting the liquid accumulation position by an adjusting plate 25 provided in the rotating body 10.
[0009]
Further, by supplying water at a predetermined time interval from the water supply device 24, the operation and stop of the pilot valve 23 are controlled, whereby the valve cylinder 16 provided therein is slid up and down to reach the maximum diameter portion. By controlling the opening and closing of the provided sludge discharge hole 13, the discharge of sludge composed of solid matter and a part of heavy liquid accumulated in the maximum diameter portion of the rotating body 10 is controlled. (For example, refer to Patent Document 1).
[0010]
Further, the separator-type centrifuge has a structure for discharging heavy liquid without a heavy liquid discharge impeller or an adjusting plate, a structure for continuously discharging sludge from a nozzle type sludge discharge hole, or a valve cylinder type sludge. An apparatus using both discharge and nozzle-type sludge discharge is generally known (for example, see Patent Document 2).
[0011]
In addition, the present invention is not applied only to the separation plate type centrifugal separator, but supplies a liquid to be treated mixed with solids into a rotating body, performs solid-liquid separation by centrifugal force, and at least separates the separated liquid. As long as it is a centrifugal separator that continuously discharges, a non-porous basket type centrifugal separator or the like can be applied.
[0012]
[Patent Document 1]
Japanese Patent Publication No. 57-034023 [Patent Document 2]
JP 2001-239184 A
[Problems to be solved by the invention]
In the solid-liquid separation method in the conventional centrifugal separator, light liquid, heavy liquid and solids are efficiently separated, and a light liquid having high clarity can be easily obtained, but when the amount of sludge increases, In the valve opening / closing type sludge discharge structure, since the number of times of opening and closing of the valve cylinder for discharging the sludge increases, the valve cylinder, the valve packing, and the like become severely worn, and there is a problem that costs and operating time loss due to replacement of parts increase. . Further, in the nozzle-type sludge discharge structure, there is a possibility that a discharge failure may occur due to accumulation of sludge in the nozzle portion. In particular, in the case of a liquid to be treated containing a solid which is easily fixed, there is a problem that the solid is fixed to the inner wall of the rotating body, making it impossible to discharge the solid. Classification by pod specific gravity is not possible.
[0014]
The present invention has been made in view of the above problems, and a liquid to be treated containing a large amount of solid matter, a liquid to be treated containing a solid matter that easily adheres, or a liquid to be treated containing a solid matter that is easily broken. Even if there is any problem, the object is to provide a solid-liquid separation method using a centrifugal separator, which can be separated and easily discharged without any trouble, and can also classify solids.
[0015]
[Means for Solving the Problems]
The gist of the present invention for achieving the above object is that, in the invention according to claim 1, a liquid to be treated mixed with a solid is supplied to a rotating body and solid-liquid separated by centrifugal force. In a centrifuge that continuously discharges, after supplying a fixed amount of a viscous substance that is difficult to dissolve in the liquid to be treated and has fluidity as a solid substance capturing agent into the rotating body, the liquid to be treated is continuously supplied. A method for separating solid and liquid by a centrifugal separator, wherein solid-liquid separation is performed by centrifugal force, the separated liquid is continuously discharged, and after a predetermined time, the supply of the liquid to be treated is stopped and the contents of the rotating body are discharged. It is.
[0016]
With the above configuration, the solid substance is hardly dissolved in the liquid to be treated and the viscous substance having fluidity is captured and retained in the solid substance capturing agent, and thereafter discharged, whereby the solid substance is rotated. There is no danger of sticking to the inner wall of the tank and causing a problem that discharge becomes impossible.Therefore, a liquid to be treated that contains a large amount of solids, a liquid to be treated that contains solids that easily adhere, or a solid that is easily broken The liquid to be treated can be separated and easily discharged without any trouble. In addition, by appropriately adjusting the viscosity and specific gravity of the solid trapping agent according to the solid, the classification operation can be performed based on the difference in sedimentation speed of the solid in the solid trapping agent.
[0017]
Further, in the invention according to claim 2, in a centrifugal separator that supplies a liquid to be treated mixed with solids into a rotating body, performs solid-liquid separation by centrifugal force, and continuously discharges at least the separated liquid, While continuously supplying a viscous substance that is difficult to dissolve in the liquid to be treated and has fluidity to the rotating body as a solid substance trapping agent, the liquid to be treated is continuously supplied and solid-liquid separated by centrifugal force. A solid-liquid separation method using a centrifugal separator, characterized by continuously discharging a solid substance capturing agent.
[0018]
According to the above configuration, the solid is hardly dissolved in the liquid to be treated and the viscous substance having fluidity is captured in the solid capturing agent, held and continuously discharged, whereby the solid is rotated. Since there is no danger of sticking to the inner wall of the body and causing a problem that discharge becomes impossible, a liquid to be treated containing a large amount of solid matter, a liquid to be treated containing a solid matter which easily adheres, or a solid matter which is easily broken is used. Even the mixed liquid to be treated can be separated and easily discharged without any trouble. In addition, by appropriately adjusting the viscosity and specific gravity of the solid trapping agent according to the solid, the classification operation can be performed based on the difference in sedimentation speed of the solid in the solid trapping agent.
[0019]
According to a third aspect of the present invention, in the solid-liquid separation method using the centrifugal separator according to the first or second aspect, the centrifugal separator is formed of a frustoconical thin plate in a rotating body. Is a solid-liquid separation method using a centrifugal separator, which is a separating plate type centrifugal separator that is internally provided by laminating a large number in the axial direction.
[0020]
According to the configuration, in addition to the effect of the first aspect, while the light liquid flows upward in the gap between the separation plates, the remaining heavy liquid and solids are further settled and separated, and clarification is efficiently promoted. Therefore, the light liquid, the heavy liquid, and the solid matter are efficiently separated, and a light liquid having high clarity can be easily obtained.
[0021]
According to a fourth aspect of the present invention, in the solid-liquid separation method using the centrifuge according to the first, second, or third aspect, the liquid to be treated is an oil mixed with a solid, This is a solid-liquid separation method using a centrifuge in which the substance trapping agent is a viscous substance prepared by dissolving a polymer flocculant in water to adjust the concentration to a predetermined concentration, and the separated liquid is clear oil.
[0022]
With the above configuration, the effects described in claim 1, claim 2, or claim 3 can be maximized.
[0023]
In the above, as the solid substance capturing agent, yam separation extract, gelatin, a biologically produced viscous substance, alginate, agar, natural polymer substances such as gelatin, polyvinyl alcohol, polyacrylic acid, synthetic polymer substances such as polyacrylamide, In addition, various coagulants used in water treatment such as anionic polymer coagulant, cationic polymer coagulant or nonionic polymer coagulant can be used. The concentration is appropriately adjusted according to the type of the solid substance in the liquid to be treated, and the liquid substance is used as a viscous substance such as a gel substance, a sol substance, or a high viscosity substance.
[0024]
When the viscosity of the solid substance capturing agent is adjusted, it is preferable to use a viscous substance having a viscosity of 10,000 to 200,000 cps, preferably 25,000 to 150,000 cps, and a specific gravity of 1.0 to 1 cps. However, the present invention is not limited thereto, as long as it is a viscous substance that is hardly dissolved in the liquid to be treated and has fluidity.
[0025]
The liquid to be treated mixed with the solid matter to be treated in the present separation method includes oils and fats such as fuel oil, waste mineral oil and used edible oil containing 0.1 to 2.0 wt% of inorganic solid matter, plankton. It can be applied to water containing microorganisms such as oils and fats or water which need to be classified by containing solids having a plurality of specific gravity differences.
[0026]
BEST MODE FOR CARRYING OUT THE INVENTION
An embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a system diagram of a solid-liquid separator showing an enlarged sectional view of a rotating body of a centrifuge according to an embodiment of the present invention, and FIG. 2 is an enlarged sectional view of a rotating body of a conventional centrifuge. is there. In FIG. 1, the same reference numerals as in FIG.
[0027]
In FIG. 1, reference numeral 1 denotes a rotating body 10 mainly composed of a rotating body 11 having a sludge discharge hole 13 in an outer peripheral portion and a rotating body lid 12 for covering the upper part of the rotating body 11 in a casing (not shown). 22 and a valve cylinder for opening and closing a separation plate group 15 and a sludge discharge hole 13 formed by laminating a large number of separation plates 14 formed of frustoconical thin plates in the rotating body 10 in the axial direction of the rotating body. 16 is a separation plate type centrifugal separator to which No. 16 is attached.
[0028]
Further, in the separation plate type centrifugal separator 1, a stock solution supply pipe 17 is inserted and mounted at an axial position of the rotating body 10, and a guide tube 20 for introducing the supplied stock solution into the separation chamber of the rotating body 10 is provided with a stock solution. A light liquid discharge impeller 18 provided concentrically with the supply pipe 17 and provided in a light liquid discharge passage for discharging the light liquid flowing upward through the gap between the separation plate groups 15, The heavy liquid provided in the heavy liquid discharge flow path passes through the heavy liquid flow path formed by the heavy liquid guide plate 21 for discharging the accumulated heavy liquid and the heavy liquid from the solid matter and the inner wall of the rotating body lid 12. An impeller 19 and an adjusting plate 25 for adjusting discharge of the light liquid and the heavy liquid are provided therein.
[0029]
Further, a hydraulic water supply device 24 and a pilot valve 23 are provided for sliding the valve cylinder 16 provided therein up and down to control opening and closing of the sludge discharge hole 13 provided in the maximum diameter portion.
[0030]
Reference numeral 2 denotes a stock solution tank for storing a liquid to be treated mixed with solids (hereinafter referred to as a stock solution), and reference numeral 3 denotes a fining solution for storing a clarified processing solution in which solids are separated by the centrifuge 1. The liquid tank No. 4 is a solid substance trapping agent tank that stores at least one solid substance trapping agent of a gel-like substance, a sol-like substance, or a high-viscosity substance that is hardly dissolved in the liquid to be treated and has fluidity. is there.
[0031]
Reference numeral 5 denotes a stock solution supply pump that supplies a stock solution from the stock solution tank 2 to the centrifuge 1, and reference numeral 6 denotes a solid material that supplies a solid material capturing agent from the solid material capturing agent tank 4 to the centrifuge 1. It is a capture agent supply pump.
[0032]
By the solid-liquid separator, for example, a method of treating a high-viscosity substance adjusted to a predetermined viscosity or specific gravity by dissolving a polymer coagulant with water as a solid solution, using a fat or oil mixed with a solid as a stock solution, The details will be described below.
[0033]
After the centrifuge 1 is operated, the polymer flocculant is dissolved in water in the solid substance trapping agent tank 4 to adjust the concentration to a predetermined specific gravity, and the adjusted gel-like fluid (hereinafter referred to as a trapping substance) is solidified. When the material capturing agent supply pump 6 supplies the raw material into the rotary body 10 from the raw material inlet 28 of the raw solution supply pipe 17 inserted and mounted at the axial position of the rotary body 10 through the solid material capturing agent supply path b, the captured substance Is stored in the maximum diameter portion of the rotating body 10, and then is pumped out by the heavy liquid impeller 19 through the heavy liquid flow path formed by the heavy liquid guide plate 21 and the inner wall of the rotating body lid 12, and the solid matter is It is circulated from the trapping agent circulation path d to the solid substance trapping agent tank 4.
[0034]
While continuing the circulation of the fluid, the stock solution is supplied from the stock solution tank 2 from the stock solution inlet 28 of the stock solution supply pipe 17 inserted and mounted at the axial position of the rotating body 10 through the stock solution supply path a by the stock solution supply pump. Then, the supplied undiluted solution is introduced into the separation chamber of the rotator 10 by descending the guide cylinder 20 and centrifugal force generated by the high speed rotation of the rotator 10 rotated via the rotation shaft causes the fat and oil (hereinafter, referred to as light grease) to have a low specific gravity. A light liquid) and a solid having a high specific gravity and a mixture of water and a solid (hereinafter referred to as a heavy liquid) are separated by a specific gravity difference.
[0035]
The separated heavy liquid and solid matter are accumulated in the largest diameter portion in the rotating body 10, and the light liquid flows upward through the gap between the separation plate group 15 and the light liquid discharge impeller provided in the light liquid discharge passage. It is pumped out by 18 and discharged out of the rotating body 10 from the light liquid outlet 26 and stored in the clarifying liquid tank 3 through the light liquid discharge channel c.
[0036]
In the separation and discharge of the light liquid, the remaining heavy liquid and solids are further settled and separated while the light liquid flows upward through the gap of the separation plate group 15, so that the clarification is efficiently performed. Will be promoted.
[0037]
When a certain amount of heavy liquid and solid liquid accumulated in the maximum diameter portion of the rotating body 10 accumulate, a heavy liquid flow path formed by the heavy liquid guide plate 21 and the inner wall of the rotating body lid 12 is formed. Then, it is pumped out by the heavy liquid impeller 19 and discharged out of the rotating body 10 from the heavy liquid outlet 27.
[0038]
The discharge of the light liquid and the heavy liquid is controlled by adjusting the accumulation position of the heavy liquid by the adjusting plate 25 provided in the rotating body 10.
[0039]
Further, by supplying water at a predetermined time interval from the water supply device 24, the operation and stop of the pilot valve 23 are controlled, whereby the valve cylinder 16 provided therein is slid up and down to reach the maximum diameter portion. By controlling the opening and closing of the sludge discharge hole 13 provided, the discharge of the sludge composed of the solid matter accumulated in the maximum diameter portion of the rotating body 10 and a part of the heavy liquid is controlled, but most of the solid matter flows. Since the sludge discharge hole 13 is captured and discharged by the animal, there is almost no need to open and close the sludge discharge hole 13, or at least the frequency of opening and closing the sludge discharge hole 13 is reduced as compared with the conventional method.
[0040]
In addition, by appropriately adjusting the viscosity and specific gravity of the solid trapping agent according to the solid, the classification operation can be performed based on the difference in the sedimentation speed of the solid in the solid trapping agent.
[0041]
【Example】
Next, an example in which turbine oil whose solid matter concentration is adjusted by the method of the present invention will be described.
Turbine oil No. 32 Kanto Loam No. 11 was adjusted to a solid concentration of 0.3 kg / m 3 to obtain a stock solution. A high-viscosity substance prepared by dissolving an anionic polymer flocculant with water and adjusting the concentration to 2 wt% was used as a solid substance capturing agent.
The test method was such that the rotating body of the separation plate type centrifuge was rotated at a centrifugal force of 11,150 G, and the solid matter trapping agent was connected to the undiluted liquid supply pipe at 2 L / Hr by a solid matter trapping agent supply pump. It was supplied into the rotating body via the capture agent supply pipe, and was discharged and circulated through the heavy liquid discharge pipe. The liquid to be treated was supplied at 100 L / Hr from a stock solution supply pipe.
[0042]
According to the above test, Kanto loam which is extremely easy to adhere to the rotating body wall is dispersed and captured in the solid matter capturing agent, discharged without being fixed to the rotating body wall surface, and to obtain clear turbine oil as light liquid. And continuous operation for a long time was possible.
[0043]
After completion of the test, the solid matter trapping agent, the turbine oil and the liquid mixed with Kanto loam in the rotating body were all collected and separated by a batch centrifugal sedimentation tube at a centrifugal force of 1,000 G. And the Kanto loam were separated into solid capture agents mixed and dispersed, and there was no sedimentation of the Kanto loam. As a result, it was found that the solid was trapped by the solid trap and was stably dispersed. It has also been found that there is no problem in circulating and using the solid matter trapping agent for a long time.
[0044]
【The invention's effect】
The present invention can separate and easily discharge a liquid to be treated containing a large amount of solids, a liquid to be treated which contains solids which are easily fixed, or a liquid which contains solids which are easily broken. And a solid-liquid separation method using a centrifugal separator that can further classify solids.
[Brief description of the drawings]
FIG. 1 is a system diagram of a solid-liquid separator showing an enlarged sectional view of a rotating body of a centrifuge according to an embodiment of the present invention. FIG. 2 is an enlarged sectional view of a rotating body of a conventional centrifuge. [Explanation of symbols]
1: separation plate type centrifugal separator 2: stock solution tank 3: clarification solution tank 4: solid matter trapping agent tank 5: stock solution supply pump 6: solid matter trapping agent supply pump 10: rotating body

Claims (4)

固形物が混入する被処理液を回転体内に供給して遠心力で固液分離し、少なくとも分離した液体を連続的に排出する遠心分離機において、被処理液に溶解しにくく且つ流動性を持つ粘稠性物質を固形物捕捉剤として回転体内に一定量供給したのち、被処理液を連続供給して遠心力で固液分離し、分離した液体を連続的に排出し、所定時間後に被処理液の供給を停止して回転体内容物を排出することを特徴とする遠心分離機による固液分離方法。In a centrifugal separator that supplies a liquid to be treated mixed with solids into a rotating body and separates it into solid and liquid by centrifugal force, and continuously discharges at least the separated liquid, it is difficult to dissolve in the liquid to be treated and has fluidity. After a certain amount of the viscous substance is supplied as a solid trapping agent into the rotating body, the liquid to be treated is continuously supplied, and solid-liquid separation is performed by centrifugal force, and the separated liquid is continuously discharged. A solid-liquid separation method using a centrifuge, wherein the supply of the liquid is stopped and the contents of the rotating body are discharged. 固形物が混入する被処理液を回転体内に供給して遠心力で固液分離し、少なくとも分離した液体を連続的に排出する遠心分離機において、被処理液に溶解しにくく且つ流動性を持つ粘稠性物質を固形物捕捉剤として回転体内に連続供給しながら、被処理液を連続供給して遠心力で固液分離し、分離した液体と固形物捕捉剤とを連続的に排出することを特徴とする遠心分離機による固液分離方法。In a centrifugal separator that supplies a liquid to be treated mixed with solids into a rotating body and separates it into solid and liquid by centrifugal force, and continuously discharges at least the separated liquid, it is difficult to dissolve in the liquid to be treated and has fluidity. While continuously supplying the viscous substance as a solid trapping agent into the rotating body, the liquid to be treated is continuously supplied and solid-liquid separated by centrifugal force, and the separated liquid and the solid trapping agent are continuously discharged. A solid-liquid separation method using a centrifuge. 前記遠心分離機が、回転体内に截頭円錐形状の薄板からなる分離板が軸方向に多数積層して内設した分離板型遠心分離機である請求項1又は請求項2に記載の遠心分離機による固液分離方法。The centrifugal separator according to claim 1 or 2, wherein the centrifugal separator is a separator-type centrifugal separator in which a plurality of frustro-conical thin plates are stacked in a rotating body in an axial direction and internally provided. Solid-liquid separation method using a machine. 前記被処理液が固形物が混入した油であり、前記固形物捕捉剤が高分子凝集剤を水で溶解して所定濃度に調整した粘稠性物質であり、分離した液体が清澄油である請求項1、請求項2又は請求項3に記載の遠心分離機による固液分離方法。The liquid to be treated is an oil mixed with solids, the solids trapping agent is a viscous substance prepared by dissolving a polymer coagulant with water to a predetermined concentration, and the separated liquid is a clear oil. A solid-liquid separation method using the centrifugal separator according to claim 1, 2 or 3.
JP2002323317A 2002-11-07 2002-11-07 Solid-liquid separation method using a centrifuge Expired - Lifetime JP4047136B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002323317A JP4047136B2 (en) 2002-11-07 2002-11-07 Solid-liquid separation method using a centrifuge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002323317A JP4047136B2 (en) 2002-11-07 2002-11-07 Solid-liquid separation method using a centrifuge

Publications (2)

Publication Number Publication Date
JP2004154694A true JP2004154694A (en) 2004-06-03
JP4047136B2 JP4047136B2 (en) 2008-02-13

Family

ID=32803207

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002323317A Expired - Lifetime JP4047136B2 (en) 2002-11-07 2002-11-07 Solid-liquid separation method using a centrifuge

Country Status (1)

Country Link
JP (1) JP4047136B2 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010526654A (en) * 2007-05-10 2010-08-05 アルファ ラヴァル コーポレイト アクチボラゲット Method and apparatus for purifying fluid in a centrifuge
JP2013534866A (en) * 2010-07-02 2013-09-09 アルファ・ラバル・コーポレイト・エービー Purification equipment for gas scrubber fluid
JP2014507490A (en) * 2010-12-16 2014-03-27 オムヤ インターナショナル アーゲー Inorganic compositions, especially for use in paper fillers and paper or plastic coatings
KR101575692B1 (en) 2008-06-18 2015-12-08 토탈 마케팅 서비스 Cylinder lubricant for a two-stroke marine engine
US9266055B2 (en) 2010-02-25 2016-02-23 Alfa Laval Corporate Ab Exhaust gas and gas scrubber fluid cleaning equipment and method
JP2018039005A (en) * 2016-03-07 2018-03-15 伯東株式会社 Processing method of crude oil-containing waste liquid and processing facility of crude oil-containing waste liquid
US9943861B2 (en) 2009-10-29 2018-04-17 Alfa Laval Corporate Ab Centrifugal separator with a control unit for speed control
CN108483820A (en) * 2018-05-29 2018-09-04 温仕鑫 A kind of equipment for processing industrial sewage and its processing method

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104096388B (en) * 2014-07-28 2015-11-04 湘潭大学 A kind of method of direct separating catalyst from solid-liquid phase reaction system

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010526654A (en) * 2007-05-10 2010-08-05 アルファ ラヴァル コーポレイト アクチボラゲット Method and apparatus for purifying fluid in a centrifuge
KR101503549B1 (en) * 2007-05-10 2015-03-17 알파 라발 코포레이트 에이비 Method and device for cleaning of a fluid in a centrifugal separator
KR101575692B1 (en) 2008-06-18 2015-12-08 토탈 마케팅 서비스 Cylinder lubricant for a two-stroke marine engine
US9943861B2 (en) 2009-10-29 2018-04-17 Alfa Laval Corporate Ab Centrifugal separator with a control unit for speed control
US9266055B2 (en) 2010-02-25 2016-02-23 Alfa Laval Corporate Ab Exhaust gas and gas scrubber fluid cleaning equipment and method
JP2013534866A (en) * 2010-07-02 2013-09-09 アルファ・ラバル・コーポレイト・エービー Purification equipment for gas scrubber fluid
JP2014507490A (en) * 2010-12-16 2014-03-27 オムヤ インターナショナル アーゲー Inorganic compositions, especially for use in paper fillers and paper or plastic coatings
JP2018039005A (en) * 2016-03-07 2018-03-15 伯東株式会社 Processing method of crude oil-containing waste liquid and processing facility of crude oil-containing waste liquid
CN108483820A (en) * 2018-05-29 2018-09-04 温仕鑫 A kind of equipment for processing industrial sewage and its processing method

Also Published As

Publication number Publication date
JP4047136B2 (en) 2008-02-13

Similar Documents

Publication Publication Date Title
KR101503549B1 (en) Method and device for cleaning of a fluid in a centrifugal separator
RU2573876C2 (en) Product phase separation by centrifuge
SE506930C2 (en) Method and apparatus for thickening fine particulate suspensions
KR20160125226A (en) Centrifugal separator and method for sludge separating using the same
JP2005013783A (en) Liquid centrifugal separator
JP2004154694A (en) Solid-liquid separating method using centrifugal separator
US4348288A (en) Process for desalting fuel oil
RU150521U1 (en) APPARATUS FOR CENTRIFUGAL SEPARATION OF A GAS-WATER-OIL MIXTURE CONTAINING SOLID IMPURITIES
EP2900798B1 (en) Continuous purification of motor oils
JP2012245466A (en) Apparatus and method for clarifying waste liquid
KR20120011990A (en) Drum type fine impurities disposal machine
KR20110094808A (en) Semiconductor wastewater treatment plant and processing system
KR20190032860A (en) Cyclone filter apparatus
JP2001277113A (en) Method and device for removing grinding wheel grain from grinding fluid
JP2595441B2 (en) Coagulation sedimentation separation equipment
SU1194460A1 (en) Method of centrifugal filtering
RU2106893C1 (en) Filter
RU200895U1 (en) APPARATUS FOR SEPARATING GAS-WATER-OIL EMULSION
JP2001179132A (en) Separating plate type centrifugal separating machine with filter
JP3483462B2 (en) Sludge removal equipment for treatment liquid for heat treatment
KR101926691B1 (en) Solid-liquid separator
JPH0632201Y2 (en) Solids separation device using a centrifuge
JPS6032669B2 (en) Fuel oil cleaning and desalination method
JPH04310255A (en) Screw type decanter
JPS6145680B2 (en)

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20050706

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20070709

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20070807

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20071005

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20071120

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20071121

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

Free format text: PAYMENT UNTIL: 20101130

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Ref document number: 4047136

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

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

Free format text: PAYMENT UNTIL: 20111130

Year of fee payment: 4

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

Free format text: PAYMENT UNTIL: 20111130

Year of fee payment: 4

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

Free format text: PAYMENT UNTIL: 20121130

Year of fee payment: 5

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

Free format text: PAYMENT UNTIL: 20121130

Year of fee payment: 5

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

Free format text: PAYMENT UNTIL: 20131130

Year of fee payment: 6

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

EXPY Cancellation because of completion of term