JP3785215B2 - Steam heating device - Google Patents

Steam heating device Download PDF

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Publication number
JP3785215B2
JP3785215B2 JP08740596A JP8740596A JP3785215B2 JP 3785215 B2 JP3785215 B2 JP 3785215B2 JP 08740596 A JP08740596 A JP 08740596A JP 8740596 A JP8740596 A JP 8740596A JP 3785215 B2 JP3785215 B2 JP 3785215B2
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Japan
Prior art keywords
heating
condensate
steam
valve
nozzle
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Expired - Fee Related
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JP08740596A
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Japanese (ja)
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JPH09250887A (en
Inventor
鎮麿 大石
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Tlv Co Ltd
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Tlv Co Ltd
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Filing date
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Priority to JP08740596A priority Critical patent/JP3785215B2/en
Publication of JPH09250887A publication Critical patent/JPH09250887A/en
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Publication of JP3785215B2 publication Critical patent/JP3785215B2/en
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Description

【0001】
【発明の属する技術分野】
本発明は熱交換器内の被加熱物を蒸気で加熱するものに関し、特にその加熱温度が100度C程度の比較的低温の場合に適した蒸気加熱装置に関する。
【0002】
【従来の技術】
従来の蒸気加熱装置としては例えば特開平7−328423号公報に示されているようなものが用いられていた。これは、加熱部の入口側に蒸気供給管と連通したノズルとその周囲に吸引室を形成して、吸引室と加熱部を接続すると共に、ノズルの出口側に弁手段を介在したものであり、100度C程度の比較的低温の蒸気によって被加熱物を加熱することができるものである。
【0003】
【発明が解決しようとする課題】
上記従来のものは、熱交換器の加熱部で発生した凝縮水としての復水を確実に吸引することができず、加熱部にその復水を滞留してしまう問題があった。加熱部で使用する蒸気圧力が低くて大気圧とほとんど差が無い場合や、加熱部と復水回収装置との間に立下げ部を設けることができないような場合には、加熱部で発生した復水が復水回収装置へ自然流下することができず、加熱部に滞留してしまうのである。
【0004】
加熱部に復水が滞留すると、復水は蒸気と比較して熱容量が小さいために、被加熱物に熱を奪われるとただちに温度低下を来たしてしまい、温度ムラを生じて被加熱物を均一に加熱することができなくなってしまうのである。
【0005】
従って本発明の技術的課題は、熱交換器の加熱部で発生した復水を確実に吸引することができるようにして、復水を滞留することがない蒸気加熱装置を得ることである。
【0006】
【課題を解決するための手段】
上記の技術的課題を解決するために講じた本発明の技術的手段は、熱交換器に加熱部を形成して加熱用の蒸気供給管を接続すると共に、加熱により生じた復水を排出する復水回収装置を接続して、加熱部の入口側に蒸気供給管と連通したノズルを配置して当該ノズルの出口側を加熱部と接続し、ノズルの周囲を覆う吸引室を形成して当該吸引室を復水回収装置と接続したものにおいて、ノズルの出口側と加熱部とを管路を介して接続し、当該管路を分岐して大気連通管と開閉弁を取り付けて、当該大気連通管と開閉弁から加熱部と復水回収装置内の残存空気を排除するものである。
【0007】
【発明の実施の形態】
ノズルに蒸気を供給することにより、その出口側から加熱部へ蒸気が供給されると共に、ノズルの周囲の吸引室で吸引力を生じ、復水回収装置内を吸引することによって、復水回収装置内は大気圧以下の真空状態となる。復水回収装置内を真空状態とすることにより、熱交換器の加熱部での蒸気圧力が低くて大気圧とほとんど差が無い場合や大気圧以下の場合、あるいは、加熱部と復水回収装置との間に立下げ部を設けることができない場合であっても、加熱部で発生した復水は確実に復水回収装置内へ流下する。
【0008】
【実施例】
本実施例においては熱交換器として反応釜1を用いた例を示す。反応釜1の外周に加熱部としてのジャケット部2を形成して蒸気供給管3を接続する。蒸気供給管3には、順次、開閉弁4と圧力調節弁5、及び、エゼクタ6を接続する。エゼクタ6は内部にノズルを有する吸引室7とディフュ―ザ8で形成して、ノズルの出口側すなわちディフュ―ザ8を管路9を介してジャケット部2と接続する。また、管路9を分岐して大気連通管10と開閉弁11を取り付ける。
【0009】
ジャケット部2の下部を管路12を介して復水回収装置16の復水流入口15と接続する。管路12には開閉弁13と、ジャケット部2から復水回収装置16側への流体の通過のみ許容する逆止弁14とを取り付ける。復水回収装置16の復水流出口17にも逆止弁18を介して復水回収管19を取り付ける。逆止弁18は、復水回収装置16から復水回収管19側への流体の通過のみを許容するものである。
【0010】
復水回収装置16の上部に、圧送流体流入口20と排気口21を設けて、圧送流体流入口20を管路22を介して蒸気供給管3と接続すると共に、排気口21は管路23を介してエゼクタ6の吸込室7と接続する。
【0011】
復水回収装置16の詳細構造を図2に示す。復水流入口15から流入してきた復水が本体25内に溜りその水位が上昇するとフロ―ト26とフロ―トレバ―27も回動ピン28を中心にして上昇する。フロ―ト26の上昇に伴い、フロ―トレバ―27に一端を取り付けた引張コイルバネ29と、回動ピン28の反対側に設けて引張コイルバネ29の他端を取り付けた揺動ア―ム30には、引張コイルバネ29の引張力が徐々に増加しながら付勢される。
【0012】
更にフロ―ト26が上昇して、フロ―トレバ―27と引張コイルバネ29と揺動ア―ム30のそれぞれの中心軸が一直線上に重なり、その位置よりフロ―トア―ム27が上方へ変位した瞬間に引張コイルバネ29の増加した引張力が揺動ア―ム30を回動ピン28を中心にして上方へ変位させることにより、揺動ア―ム30に取り付けた弁棒31を上方へスナップ移動させる。
【0013】
弁棒31の上端に、圧送弁32と排気弁33を取り付けておくことにより、フロ―ト26の上昇、すなわち、本体25内への復水の滞留によって圧送弁32が開弁し、排気弁33が閉弁する。反対にフロ―ト26の降下によって図2に示すように、圧送弁32が閉弁し排気弁33が開弁するものである。
【0014】
図1において、蒸気供給管3からエゼクタ6を介して反応釜1のジャケット部2へ加熱用の蒸気を供給することにより、反応釜1内の被加熱物が加熱される。加熱蒸気温度は圧力調節弁5によって蒸気圧力を調節することにより、蒸気の圧力と温度は1対1の関係があるために、任意に調節することができる。加熱により熱を奪われた蒸気は凝縮して復水となる。
【0015】
エゼクタ6を蒸気が通過することにより吸引室7では吸引力を生じ、管路23を介して復水回収装置16内を所定の真空状態とすることによって、ジャケット部2で発生した復水は滞留することなく復水回収装置16内へ流下する。復水回収装置16内の水位が所定レベルに達すると図2における弁棒31がスナップ移動して、圧送弁32を開弁すると共に排気弁33を閉弁することによって、管路22から本体25内へ高圧蒸気が供給され、本体25内の復水は逆止弁18を介して回収先へ圧送される。
【0016】
復水が圧送され復水回収装置16内の水位が低下すると、弁棒31が逆方向へスナップ移動することにより、圧送弁32が閉弁し排気弁33が開弁して、再度ジャケット部2内の復水を吸引する。上記の作動サイクルを繰り返して反応釜1を低温の蒸気で加熱する。
【0017】
蒸気加熱を行う場合、蒸気中に空気等の不凝縮ガスが混入すると、その伝熱効率が極端に低下する。また、加熱を開始する初期の段階においては、加熱装置内には多量の空気が残存しているのが一般的である。この様な場合に、エゼクタ6に蒸気を通過させながら、開閉弁35,13,36を開弁させ、続いて開閉弁35を閉弁させ開閉弁11を開弁させることにより、エゼクタ6の吸引室7へジャケット部2と復水回収装置16内に残存していた空気を、大気連通管10を介して排除することができ、蒸気加熱装置での伝熱効率の低下を防止することができる。
【0018】
【発明の効果】
上記のように本発明によれば、ノズルと吸引室で復水回収装置の内部を大気圧以下の真空状態とすることができ、復水回収装置内へ復水を確実に流下させて、熱交換器の加熱部に復水を滞留することがなく、従って、熱交換器の被加熱物に温度ムラを生じることがなく均一に加熱することができる。
【図面の簡単な説明】
【図1】本発明の蒸気加熱装置の実施例を示す構成図である。
【図2】本発明の蒸気加熱装置に用いる復水回収装置の構成図である。
【符号の説明】
1 反応釜
2 ジャケット部
3 蒸気供給管
6 エゼクタ
7 吸引室
8 ディフュ―ザ
14 逆止弁
15 復水流入口
16 復水回収装置
17 復水流出口
18 逆止弁
20 圧送流体流入口
21 排気口
26 フロ―ト
29 引張コイルバネ
31 弁棒
32 圧送弁
33 排気弁
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to an apparatus for heating an object to be heated in a heat exchanger with steam, and more particularly to a steam heating apparatus suitable for heating at a relatively low temperature of about 100 ° C.
[0002]
[Prior art]
As a conventional steam heating device, for example, a device as disclosed in JP-A-7-328423 has been used. This is a nozzle connected to the steam supply pipe on the inlet side of the heating section and a suction chamber formed around the nozzle, connecting the suction chamber and the heating section, and interposing a valve means on the outlet side of the nozzle. The object to be heated can be heated by steam at a relatively low temperature of about 100 ° C.
[0003]
[Problems to be solved by the invention]
The conventional apparatus has a problem that the condensed water as the condensed water generated in the heating section of the heat exchanger cannot be reliably sucked, and the condensed water stays in the heating section. When the steam pressure used in the heating unit is low and there is almost no difference from the atmospheric pressure, or when it is not possible to provide a falling part between the heating unit and the condensate recovery device, it occurred in the heating unit Condensate cannot naturally flow down to the condensate recovery device and stays in the heating section.
[0004]
If the condensate stays in the heating section, the heat capacity of the condensate is smaller than that of the steam.As a result, when the object to be heated is deprived of heat, the temperature immediately drops, causing temperature unevenness and uniforming the object to be heated. It becomes impossible to heat it.
[0005]
Therefore, the technical problem of the present invention is to obtain a steam heating device that can reliably suck the condensate generated in the heating section of the heat exchanger and does not retain the condensate.
[0006]
[Means for Solving the Problems]
The technical means of the present invention taken to solve the above technical problem is to form a heating section in a heat exchanger and connect a heating steam supply pipe and discharge condensate generated by heating. connect the condensate recovery system, to the inlet side of the heating section by arranging the nozzles in communication with the steam supply pipe connected to the heating unit to an outlet side of the nozzle, the forming a suction chamber covering the periphery of the nozzle In the case where the suction chamber is connected to the condensate recovery device , the outlet side of the nozzle and the heating unit are connected via a pipe, the pipe is branched, an atmosphere communication pipe and an open / close valve are attached, and the atmosphere communication is provided. Residual air in the heating unit and condensate recovery device is excluded from the pipe and the on-off valve .
[0007]
DETAILED DESCRIPTION OF THE INVENTION
By supplying the steam to the nozzle, the steam is supplied from the outlet side to the heating unit, and at the same time, a suction force is generated in the suction chamber around the nozzle, and the condensate recovery apparatus is sucked to recover the condensate recovery apparatus. The inside is in a vacuum state below atmospheric pressure. By setting the inside of the condensate recovery device in a vacuum state, when the steam pressure in the heating section of the heat exchanger is low and there is almost no difference from the atmospheric pressure, or when it is below atmospheric pressure, or the heating section and the condensate recovery device Even if the falling part cannot be provided between the two, the condensate generated in the heating part surely flows down into the condensate recovery apparatus.
[0008]
【Example】
In this embodiment, an example in which the reaction kettle 1 is used as a heat exchanger will be shown. A jacket portion 2 as a heating portion is formed on the outer periphery of the reaction kettle 1 and a steam supply pipe 3 is connected thereto. The steam supply pipe 3 is connected with an open / close valve 4, a pressure control valve 5, and an ejector 6 in sequence. The ejector 6 is formed by a suction chamber 7 having a nozzle inside and a diffuser 8, and connects the outlet side of the nozzle, that is, the diffuser 8 to the jacket portion 2 through a conduit 9. Further, the pipe 9 is branched and an atmosphere communication pipe 10 and an opening / closing valve 11 are attached.
[0009]
The lower part of the jacket part 2 is connected to the condensate inlet 15 of the condensate recovery apparatus 16 via the pipe line 12. An open / close valve 13 and a check valve 14 that allows only passage of fluid from the jacket portion 2 to the condensate recovery device 16 are attached to the pipe 12. A condensate recovery pipe 19 is also attached to the condensate outlet 17 of the condensate recovery device 16 via a check valve 18. The check valve 18 allows only passage of fluid from the condensate recovery device 16 to the condensate recovery pipe 19 side.
[0010]
A pumping fluid inlet 20 and an exhaust port 21 are provided in the upper part of the condensate recovery device 16, and the pumping fluid inlet 20 is connected to the steam supply pipe 3 through a pipeline 22, and the exhaust port 21 is connected to a pipeline 23. Is connected to the suction chamber 7 of the ejector 6.
[0011]
The detailed structure of the condensate recovery device 16 is shown in FIG. When the condensate flowing in from the condensate inlet 15 accumulates in the main body 25 and the water level rises, the float 26 and the flow trevor 27 also rise around the rotation pin 28. As the float 26 moves up, a tension coil spring 29 having one end attached to the flow lever 27 and a swing arm 30 provided on the opposite side of the rotating pin 28 and having the other end of the tension coil spring 29 attached thereto. Is biased while the tensile force of the tension coil spring 29 gradually increases.
[0012]
Further, the float 26 rises, and the central axes of the flow lever 27, the tension coil spring 29, and the swing arm 30 overlap each other, and the float arm 27 is displaced upward from the position. At the moment, the increased tensile force of the tension coil spring 29 displaces the swing arm 30 upward about the pivot pin 28, thereby snapping the valve stem 31 attached to the swing arm 30 upward. Move.
[0013]
By attaching the pressure feed valve 32 and the exhaust valve 33 to the upper end of the valve rod 31, the pressure feed valve 32 is opened due to the rise of the float 26, that is, the retention of condensate in the main body 25. 33 closes. On the contrary, when the float 26 is lowered, the pressure feed valve 32 is closed and the exhaust valve 33 is opened, as shown in FIG.
[0014]
In FIG. 1, by supplying steam for heating from the steam supply pipe 3 to the jacket portion 2 of the reaction kettle 1 through the ejector 6, the object to be heated in the reaction kettle 1 is heated. The heating steam temperature can be arbitrarily adjusted by adjusting the steam pressure by the pressure control valve 5 because the steam pressure and temperature have a one-to-one relationship. Steam deprived of heat by heating condenses into condensate.
[0015]
As the steam passes through the ejector 6, a suction force is generated in the suction chamber 7, and the condensate generated in the jacket portion 2 is retained by making the inside of the condensate recovery device 16 in a predetermined vacuum state via the pipe line 23. It flows down into the condensate recovery device 16 without doing so. When the water level in the condensate recovery device 16 reaches a predetermined level, the valve rod 31 in FIG. 2 snaps, opens the pressure feed valve 32 and closes the exhaust valve 33, thereby closing the main body 25 from the pipe line 22. High-pressure steam is supplied into the main body 25, and the condensate in the main body 25 is pumped to the collection destination via the check valve 18.
[0016]
When the condensate is pumped and the water level in the condensate recovery device 16 is lowered, the valve rod 31 snaps in the reverse direction, whereby the pumping valve 32 is closed and the exhaust valve 33 is opened. Aspirate the condensate inside. The above operation cycle is repeated to heat the reaction kettle 1 with low temperature steam.
[0017]
When performing steam heating, if non-condensable gas such as air is mixed in the steam, the heat transfer efficiency is extremely lowered. Further, in the initial stage of starting heating, a large amount of air generally remains in the heating device. In such a case, the suction of the ejector 6 is performed by opening the on-off valves 35, 13, and 36 while allowing the steam to pass through the ejector 6, and then closing the on-off valve 35 and opening the on-off valve 11. The air remaining in the jacket portion 2 and the condensate recovery device 16 to the chamber 7 can be eliminated via the atmosphere communication pipe 10, and a decrease in heat transfer efficiency in the steam heating device can be prevented.
[0018]
【The invention's effect】
As described above, according to the present invention, the inside of the condensate recovery device can be brought into a vacuum state of atmospheric pressure or less by the nozzle and the suction chamber, and the condensate is surely flowed down into the condensate recovery device, Condensate is not retained in the heating section of the exchanger, and therefore, the heated object of the heat exchanger can be heated uniformly without causing temperature unevenness.
[Brief description of the drawings]
FIG. 1 is a configuration diagram showing an embodiment of a steam heating apparatus of the present invention.
FIG. 2 is a configuration diagram of a condensate recovery device used in the steam heating device of the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Reaction kettle 2 Jacket part 3 Steam supply pipe 6 Ejector 7 Suction chamber 8 Diffuser 14 Check valve 15 Condensate inlet 16 Condensate recovery device 17 Condensate outlet 18 Check valve 20 Pumping fluid inlet 21 Exhaust outlet 26 Flow -G 29 Tension coil spring 31 Valve rod 32 Pressure feed valve 33 Exhaust valve

Claims (1)

熱交換器に加熱部を形成して加熱用の蒸気供給管を接続すると共に、加熱により生じた復水を排出する復水回収装置を接続して、加熱部の入口側に蒸気供給管と連通したノズルを配置して当該ノズルの出口側を加熱部と接続し、ノズルの周囲を覆う吸引室を形成して当該吸引室を復水回収装置と接続したものにおいて、ノズルの出口側と加熱部とを管路を介して接続し、当該管路を分岐して大気連通管と開閉弁を取り付けて、当該大気連通管と開閉弁から加熱部と復水回収装置内の残存空気を排除することを特徴とする蒸気加熱装置。With connecting steam supply pipe for heating forms a heating unit to the heat exchanger, connecting the condensate collecting device for discharging condensate produced by heating, communicates with the steam supply pipe to the inlet side of the heating unit It was placed a nozzle connected to the heating unit to an outlet side of the nozzle, in forming a suction chamber covering the periphery of the nozzle that connects the suction chamber and the condensate collecting device, outlet and heating of the nozzle Are connected via a pipe line, the pipe is branched, an atmospheric communication pipe and an on-off valve are attached, and residual air in the heating unit and the condensate recovery device is excluded from the atmospheric communication pipe and the on-off valve. A steam heating device characterized by.
JP08740596A 1996-03-15 1996-03-15 Steam heating device Expired - Fee Related JP3785215B2 (en)

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Application Number Priority Date Filing Date Title
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JPH09250887A JPH09250887A (en) 1997-09-22
JP3785215B2 true JP3785215B2 (en) 2006-06-14

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4540772B2 (en) * 1999-10-15 2010-09-08 株式会社テイエルブイ Steam heating device
JP4540771B2 (en) * 1999-10-15 2010-09-08 株式会社テイエルブイ Steam heating device
JP4330730B2 (en) * 1999-10-15 2009-09-16 株式会社テイエルブイ Steam heating device
US6739288B1 (en) * 2000-01-14 2004-05-25 Tvl Co., Ltd. Steam heating device
JP5047425B2 (en) * 2001-04-13 2012-10-10 株式会社テイエルブイ Steam heating device
JP5047426B2 (en) * 2001-04-13 2012-10-10 株式会社テイエルブイ Steam heating device
JP2007218472A (en) * 2006-02-15 2007-08-30 Tlv Co Ltd Waste heat-recovering/pressure-reducing device for steam
JP2007332861A (en) * 2006-06-15 2007-12-27 Tlv Co Ltd Steam ejector
JP2008150996A (en) * 2006-12-15 2008-07-03 Tlv Co Ltd Steam ejector
JP7387164B2 (en) * 2020-01-21 2023-11-28 株式会社テイエルブイ Liquid pumping device

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JP2630869B2 (en) * 1991-06-14 1997-07-16 株式会社テイエルブイ Vacuum steam generator
JPH085009A (en) * 1994-06-15 1996-01-12 Tlv Co Ltd Condensed water recovering device
JP3281999B2 (en) * 1994-06-15 2002-05-13 株式会社テイエルブイ Steam heating device

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