JPH08170886A - Steam heater - Google Patents

Steam heater

Info

Publication number
JPH08170886A
JPH08170886A JP33394094A JP33394094A JPH08170886A JP H08170886 A JPH08170886 A JP H08170886A JP 33394094 A JP33394094 A JP 33394094A JP 33394094 A JP33394094 A JP 33394094A JP H08170886 A JPH08170886 A JP H08170886A
Authority
JP
Japan
Prior art keywords
heating
steam
receiver
condensate
heat exchanger
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
JP33394094A
Other languages
Japanese (ja)
Other versions
JP3282005B2 (en
Inventor
Takayuki Morii
高之 森井
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.)
TLV Co Ltd
Original Assignee
TLV Co 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 TLV Co Ltd filed Critical TLV Co Ltd
Priority to JP33394094A priority Critical patent/JP3282005B2/en
Publication of JPH08170886A publication Critical patent/JPH08170886A/en
Application granted granted Critical
Publication of JP3282005B2 publication Critical patent/JP3282005B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

PURPOSE: To obtain a steam heater which can heat a material to be heated with steam at 100 deg.C or so uniformly and precisely and can preset a heating temperature at will. CONSTITUTION: A steam-feeding pipe 2 for heating is connected with a heat- exchanger 1. A condensed water storage part 7 is connected with the lower part of the heat-exchanger 1 through a steam trap 4. A down pipe 8 is provided at a side part of the condensed water storage part 7 and the lower end thereof is allowed to communicate within a receiver 11. A vacuum regulating valve 25 is provided at the upper end of the down pipe 8 through a pipe line 23. An opening and closing valve 13 and an air vent 12 are provided at the upper part of the receiver 11. The lower part of the receiver 11 is connected with a suction port 16 for a circulating pump 15 and a discharge port 17 therefor is connected with the lower end of the condensed water storage part 7 through a pipe line 18.

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。具体的には重合反応等に用いられる各種反応釜や
食品の蒸溜装置、濃縮装置、あるいは殺菌装置等の蒸気
加熱に用いるものである。これらの場合の被加熱物は、
少しの温度上昇によって熱損傷を生じてしまう場合が多
く、加熱温度を精度良く維持する必要がある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to heating an object to be heated in a heat exchanger with steam, and particularly, the heating temperature thereof is 100.
The present invention relates to a steam heating device suitable for a relatively low temperature of about C. Specifically, it is used for steam heating of various reaction kettles used for polymerization reaction, food distilling devices, concentrating devices, sterilizing devices, and the like. The object to be heated in these cases is
In most cases, a slight temperature rise causes thermal damage, and it is necessary to maintain the heating temperature with high accuracy.

【0002】[0002]

【従来の技術】従来の蒸気加熱装置は例えば図2に示す
ようなものが用いられていた。これは、熱交換器1を加
熱するもので、熱交換器1に加熱用の蒸気供給管2を接
続すると共に、加熱により生じた復水を排出する立下げ
部3とスチ―ムトラップ4とで復水排出装置5を構成し
たもので、蒸気供給管2から比較的低圧力すなわち低温
度の蒸気を熱交換器1へ供給することにより、熱交換器
1内の被加熱物を加熱するものである。熱交換器1内へ
供給された蒸気が加熱により凝縮して熱交換器1内を大
気圧以下程度の低圧力状態に維持することにより、10
0度Cあるいは100度C以下の比較的低温度で蒸気加
熱することができるものである。
2. Description of the Related Art For example, a conventional steam heating device as shown in FIG. 2 has been used. This heats the heat exchanger 1. The steam supply pipe 2 for heating is connected to the heat exchanger 1, and the falling portion 3 and the steam trap 4 for discharging the condensate generated by the heating are used. The condensate discharge device 5 is configured to heat the object to be heated in the heat exchanger 1 by supplying the steam having a relatively low pressure, that is, a low temperature, from the steam supply pipe 2 to the heat exchanger 1. is there. The steam supplied to the inside of the heat exchanger 1 is condensed by heating to maintain the inside of the heat exchanger 1 at a low pressure below atmospheric pressure.
Steam heating can be performed at a relatively low temperature of 0 ° C. or 100 ° C. or less.

【0003】[0003]

【発明が解決しようとする課題】上記従来の蒸気加熱装
置では、加熱用の蒸気に混入している不凝縮ガス例えば
空気等を熱交換器内から排除することができずに、加熱
温度ムラを生じて加熱温度を精度良く維持することがで
きない問題があった。
In the above-described conventional steam heating device, the non-condensable gas such as air mixed in the steam for heating cannot be removed from the heat exchanger, resulting in uneven heating temperature. There was a problem that the heating temperature could not be maintained with high accuracy.

【0004】加熱用の蒸気は少なからず幾らかの空気を
混入しているのであるが、上記従来の蒸気加熱装置で
は、復水排出装置5を立下げ部3とスチ―ムトラップ4
とで構成しているために、復水は立下げ部3に溜った水
頭圧によりスチ―ムトラップ4を通過して排出されるの
であるが、空気等の不凝縮ガスは立下げ部3に溜ること
がなく器外へ排除されないのである。
The heating steam contains some air, but not a little, but in the conventional steam heating apparatus described above, the condensate discharge device 5 is placed in the falling portion 3 and the steam trap 4.
Therefore, the condensate is discharged through the steam trap 4 by the water head pressure accumulated in the falling portion 3, but the non-condensable gas such as air is accumulated in the falling portion 3. There is no such thing and it is not excluded from the outside.

【0005】従って本発明の技術的課題は、熱交換器内
に混入した空気等の不凝縮ガスを排除することができ、
加熱温度を精度良く維持することのできる蒸気加熱装置
を提供することである。
Therefore, the technical problem of the present invention is to eliminate non-condensable gas such as air mixed in the heat exchanger,
An object of the present invention is to provide a steam heating device capable of maintaining a heating temperature with high accuracy.

【0006】[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排出装置を接続し
たものにおいて、復水排出装置に復水溜部を接続して、
当該復水溜部に所望の長さを有する立下がり部を介して
レシ―バ―を接続すると共に、当該レシ―バ―と復水溜
部とを循環ポンプを介して連通し、上記復水溜部または
立下がり部に真空度調節弁を取り付けたものである。
Means for Solving the Problems The technical means of the present invention taken to solve the above technical problems is to form a heating portion in a heat exchanger to connect a steam supply pipe for heating,
In the case where a condensate discharge device for discharging condensed water generated by heating is connected, a condensate reservoir is connected to the condensate discharge device,
A receiver is connected to the condensate reservoir via a falling part having a desired length, and the receiver and the condensate reservoir are communicated with each other via a circulation pump to form the condensate reservoir or A vacuum control valve is attached to the falling part.

【0007】[0007]

【作用】上記の技術的手段の作用は下記の通りである。
熱交換器へ供給された加熱用の蒸気は被加熱物を加熱す
ることにより凝縮して復水となり復水溜部に至る。復水
溜部と立下がり部とレシ―バ―に溜った復水を循環ポン
プで強制的に再度復水溜部へ循環させることにより、復
水溜部に流下してきた空気等の不凝縮ガスは復水の循環
流に混入してレシ―バ―に至る。
The operation of the above technical means is as follows.
The heating steam supplied to the heat exchanger condenses by heating the object to be heated and becomes condensed water, which reaches the condensed water reservoir. Non-condensable gas such as air that has flowed down to the condensate reservoir is condensed by forcibly circulating the condensate collected in the condensate reservoir, the falling part and the receiver to the condensate reservoir again. It mixes with the circulation flow of the water and reaches the receiver.

【0008】レシ―バ―内の不凝縮ガスは、ガスの発生
量が少ない場合はレシ―バ―内に溜め置き、加熱工程が
完了後に手動で外部に排除したり、あるいは、不凝縮ガ
スの存在をフロ―ト等で検知して弁口から不凝縮ガスだ
けを自動的に排出するエア―ベント等をレシ―バ―に取
り付けることにより外部に排除することができる。
When the amount of gas generated is small, the non-condensable gas in the receiver is stored in the receiver and manually discharged to the outside after the heating process is completed, or the non-condensed gas is discharged. It can be excluded to the outside by installing an air vent or the like, which detects the presence by a float or the like and automatically discharges only the non-condensable gas from the valve port, to the receiver.

【0009】復水溜部または立下がり部に真空度調節弁
を取り付けたことにより、真空度調節弁を適宜操作して
真空度を調節することによって、立下がり部や復水溜部
ひいては熱交換器内の真空度を任意に調節することがで
き、加熱用蒸気の温度を被加熱物に応じて変更すること
ができる。
By attaching a vacuum degree control valve to the condensate reservoir or the fall portion, the vacuum degree control valve is appropriately operated to adjust the degree of vacuum, so that the fall portion, the condensate reservoir portion, and the inside of the heat exchanger can be controlled. The degree of vacuum can be arbitrarily adjusted, and the temperature of the heating steam can be changed according to the object to be heated.

【0010】[0010]

【実施例】上記の技術的手段の具体例を示す実施例を図
1に基き説明する。本実施例において従来技術と同一部
材には同一符号を付す。蒸気加熱装置としての熱交換器
1に蒸気供給管2を圧力調整弁6を介して接続する。熱
交換器1の下部には復水排出装置としてのスチ―ムトラ
ップ4を取り付ける。スチ―ムトラップ4の下部に復水
溜部7を接続する。復水溜部7は断面円筒状でその側部
に所定の長さを有する立下がり部8を取り付ける。立下
がり部8の上部には開閉弁9を取り付けると共に、その
下端10をレシ―バ―11内に開口して配置する。レシ
―バ―11も円筒状のタンクとして上部にエア―ベント
12と開閉弁13を取り付け、下部には水を補給するた
めの補給水管14を接続すると共に、循環ポンプ15の
吸込口16を接続する。循環ポンプ15の吐出口17は
管路18を介して復水溜部7の下端と接続する。
EXAMPLE An example showing a concrete example of the above technical means will be described with reference to FIG. In this embodiment, the same members as those in the conventional technique are designated by the same reference numerals. A steam supply pipe 2 is connected to a heat exchanger 1 as a steam heating device via a pressure adjusting valve 6. A steam trap 4 as a condensate discharge device is attached to the lower part of the heat exchanger 1. A condensate reservoir 7 is connected to the bottom of the steam trap 4. The condensate reservoir portion 7 has a cylindrical cross section, and a falling portion 8 having a predetermined length is attached to the side portion thereof. An opening / closing valve 9 is attached to the upper portion of the falling portion 8 and a lower end 10 thereof is opened in the receiver 11. The receiver 11 is also a cylindrical tank with an air vent 12 and an opening / closing valve 13 attached to the upper part, a makeup water pipe 14 for replenishing water is connected to the lower part, and a suction port 16 of a circulation pump 15 is connected. To do. The outlet 17 of the circulation pump 15 is connected to the lower end of the condensate reservoir 7 via a pipe line 18.

【0011】復水溜部7と立下がり部8の間の連通路2
2に管路23と開閉弁24を介して真空度調節弁25を
取り付ける。真空度調節弁25は周知の自力式圧力調節
弁を用いることができ、管路23側の圧力が設定圧力よ
りも低下するとその主弁が開口して入口26側から大気
を吸引して復水溜部7及び立下がり部8へ供給すること
により、復水溜部7内ひいては熱交換器1内を所定の真
空圧力に維持するものである。真空度調節弁25として
本実施例においては自力式圧力調節弁を用いた例を示し
たが、その他周知の圧力センサ―と他力式圧力調節弁と
を組み合わせて用いることもできる。
A communication passage 2 between the condensate reservoir 7 and the falling portion 8
A vacuum degree control valve 25 is attached to 2 through a pipe line 23 and an opening / closing valve 24. A well-known self-operated pressure control valve can be used as the vacuum degree control valve 25, and when the pressure on the side of the pipe line 23 becomes lower than the set pressure, the main valve opens and sucks the atmosphere from the side of the inlet 26 to collect the condensed water. By supplying to the part 7 and the falling part 8, the inside of the condensate reservoir part 7 and hence the heat exchanger 1 is maintained at a predetermined vacuum pressure. In this embodiment, as the vacuum degree control valve 25, an example in which a self-powered pressure control valve is used is shown, but other known pressure sensors and other force type pressure control valves may be used in combination.

【0012】復水溜部7の上部には管路20と開閉弁2
1を取り付ける。開閉弁21を開弁状態とすることによ
り復水溜部7内を大気と連通状態とし、閉弁状態とする
ことにより大気と遮断状態とするものである。
A pipe 20 and an on-off valve 2 are provided above the condensate reservoir 7.
Attach 1. The open / close valve 21 is opened to bring the inside of the condensate reservoir portion 7 into communication with the atmosphere, and the valve closed state is cut off from the atmosphere.

【0013】真空度調節弁25の設定圧力は、復水溜部
7内の圧力が熱交換器1内で必要とする圧力よりもわず
かに低くなるように設定する。例えば、熱交換器1内で
360ミリメ―トル水銀柱の圧力が必要である場合、復
水溜部7内の圧力は復水等が流下するためにはそれより
低い値でなければならず、例えば、290ミリメ―トル
水銀柱に設定する。立下がり部8の長さは通常10メ―
トル程度の長さとするのが望ましい。
The set pressure of the vacuum control valve 25 is set so that the pressure in the condensate reservoir 7 is slightly lower than the pressure required in the heat exchanger 1. For example, when a pressure of 360 mm mercury column is required in the heat exchanger 1, the pressure in the condensate reservoir 7 must be lower than that for condensate to flow down. Set to 290 mm mercury column. The length of the falling portion 8 is usually 10 meters.
It is desirable to have a length of about torr.

【0014】次に作用を説明する。熱交換器1で加熱を
行う前に復水溜部7内の残存空気を除去しておく必要が
ある場合は、まず開閉弁21を開弁状態として、循環ポ
ンプ15を駆動してレシ―バ―11内の水を復水溜部7
に供給し、開閉弁21から残存空気を除去した後開閉弁
21を閉弁状態にし水がレシ―バ―11内へ自重で流下
することにより、復水溜部7の上部に所定の真空圧力域
を形成してから加熱を行う。加熱の前に残存空気の除去
が必要でない場合は上記操作は必要無い。
Next, the operation will be described. If it is necessary to remove the residual air in the condensate reservoir 7 before heating with the heat exchanger 1, first the open / close valve 21 is opened and the circulation pump 15 is driven to receive the receiver. Condensate reservoir 7
After the residual air is removed from the on-off valve 21, the on-off valve 21 is closed and the water flows down into the receiver 11 by its own weight. Is formed and then heated. If it is not necessary to remove residual air before heating, the above operation is not necessary.

【0015】蒸気供給管2から圧力調整弁6を経て供給
された低圧の加熱用蒸気は、熱交換器1内で図示しない
被加熱物を加熱することにより凝縮して復水となり、ス
チ―ムトラップ4から復水溜部7内へ流下する。復水溜
部7内に溜った復水は循環ポンプ15から供給されたレ
シ―バ―11内の循環流体の一部と共に立下がり部8を
流下してレシ―バ―11内へ至る。この場合、加熱用の
蒸気に混入してきた空気等の不凝縮ガスは、復水と共に
復水溜部7内に至り、循環流体に巻込まれて立下がり部
8を流下してレシ―バ―11の上部に溜り、エア―ベン
ト12または開閉弁13を経て外部に排除される。
The low-pressure heating steam supplied from the steam supply pipe 2 through the pressure adjusting valve 6 is condensed by heating an object to be heated (not shown) in the heat exchanger 1 to become condensed water, and a steam trap is formed. From 4 to the condensate reservoir 7. Condensed water accumulated in the condensate reservoir 7 flows down the falling portion 8 together with a part of the circulating fluid in the receiver 11 supplied from the circulation pump 15 and reaches the inside of the receiver 11. In this case, the non-condensable gas such as air mixed in the heating steam reaches the condensate reservoir 7 together with the condensate, is entrained in the circulating fluid and flows down the falling part 8 to pass through the receiver 11. It collects in the upper part and is discharged to the outside through the air vent 12 or the on-off valve 13.

【0016】レシ―バ―11内の復水の量が所定以上に
達すると図示しない排出管から外部へ排出したり、循環
ポンプ15の吐出口17を分岐した同じく図示しない分
岐管から外部へ排出する。また、循環流体の温度が所定
以上に達して循環ポンプ15に悪影響を及ぼす可能性が
生じた場合は、補給水管14から冷却水を供給して所望
温度とすることができる。
When the amount of condensed water in the receiver 11 reaches a predetermined amount or more, it is discharged to the outside from a discharge pipe (not shown) or to the outside from a branch pipe (not shown) that branches the discharge port 17 of the circulation pump 15. To do. Further, when the temperature of the circulating fluid reaches a predetermined temperature or higher and may adversely affect the circulation pump 15, cooling water can be supplied from the makeup water pipe 14 to reach the desired temperature.

【0017】[0017]

【発明の効果】上記のように本発明によれば、熱交換器
に復水溜部と立下がり部とレシ―バ―と循環ポンプを順
次接続して復水溜部の復水を強制的に循環することによ
り、復水と共に空気等の不凝縮ガスもレシ―バ―まで流
下させることができ、従って、熱交換器内の不凝縮ガス
を循環流で排除して、熱交換器内で加熱ムラを生じるこ
とがない。
As described above, according to the present invention, the condensate reservoir, the falling portion, the receiver and the circulation pump are sequentially connected to the heat exchanger to forcibly circulate the condensate in the condensate reservoir. By doing so, the non-condensable gas such as air can be made to flow down to the receiver together with the condensate. Therefore, the non-condensable gas in the heat exchanger can be eliminated by the circulation flow, and the heating unevenness in the heat exchanger can be eliminated. Does not occur.

【0018】真空度調節弁を取り付けたことにより、熱
交換器内の真空度を被加熱物に応じて任意に設定するこ
とができ、多種多様な被加熱物であっても任意に加熱温
度を設定して加熱ムラを防止することができる。
By attaching the vacuum degree control valve, the degree of vacuum in the heat exchanger can be arbitrarily set according to the object to be heated, and the heating temperature can be arbitrarily set even for various kinds of objects to be heated. It can be set to prevent uneven heating.

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

【図1】本発明の蒸気加熱装置の実施例の構成図であ
る。
FIG. 1 is a configuration diagram of an embodiment of a steam heating device of the present invention.

【図2】蒸気加熱装置の従来例を示す構成図である。FIG. 2 is a configuration diagram showing a conventional example of a steam heating device.

【符号の説明】[Explanation of symbols]

1 熱交換器 2 蒸気供給管 4 スチ―ムトラップ 7 復水溜部 8 立下がり部 11 レシ―バ― 15 循環ポンプ 25 真空度調節弁 1 heat exchanger 2 steam supply pipe 4 steam trap 7 condensate reservoir 8 falling part 11 receiver 15 circulation pump 25 vacuum control valve

Claims (1)

【特許請求の範囲】[Claims] 【請求項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
出する復水排出装置を接続したものにおいて、復水排出
装置に復水溜部を接続して、当該復水溜部に所望の長さ
を有する立下がり部を介してレシ―バ―を接続すると共
に、当該レシ―バ―と復水溜部とを循環ポンプを介して
連通し、上記復水溜部または立下がり部に真空度調節弁
を取り付けたことを特徴とする蒸気加熱装置。
1. A condensate discharge device in which a heating part is formed in a heat exchanger, a steam supply pipe for heating is connected, and a condensate discharge device for discharging condensed water generated by heating is connected. Connect the condensate reservoir, connect the receiver to the condensate reservoir via a falling part having a desired length, and connect the receiver and the condensate reservoir via a circulation pump. A steam heating device, characterized in that a vacuum control valve is attached to the condensate storage part or the falling part in communication.
JP33394094A 1994-12-15 1994-12-15 Steam heating device Expired - Fee Related JP3282005B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33394094A JP3282005B2 (en) 1994-12-15 1994-12-15 Steam heating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33394094A JP3282005B2 (en) 1994-12-15 1994-12-15 Steam heating device

Publications (2)

Publication Number Publication Date
JPH08170886A true JPH08170886A (en) 1996-07-02
JP3282005B2 JP3282005B2 (en) 2002-05-13

Family

ID=18271682

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33394094A Expired - Fee Related JP3282005B2 (en) 1994-12-15 1994-12-15 Steam heating device

Country Status (1)

Country Link
JP (1) JP3282005B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014009841A (en) * 2012-06-28 2014-01-20 Tlv Co Ltd Re-evaporation apparatus for condensate
JP2014504715A (en) * 2010-12-28 2014-02-24 ジュヒョク イム Automatic water supply steam generator using steam pressure

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014504715A (en) * 2010-12-28 2014-02-24 ジュヒョク イム Automatic water supply steam generator using steam pressure
JP2014009841A (en) * 2012-06-28 2014-01-20 Tlv Co Ltd Re-evaporation apparatus for condensate

Also Published As

Publication number Publication date
JP3282005B2 (en) 2002-05-13

Similar Documents

Publication Publication Date Title
KR100470880B1 (en) Steam heating device
JPH08170886A (en) Steam heater
JPH08170885A (en) Steam heater
JPH08170887A (en) Steam heater
JPH07328423A (en) Heater by steam
JP3510010B2 (en) Vacuum steam heating device
JPH09250705A (en) Pressure reduction steam generating device
JP2001201274A (en) Steam-heating equipment
JP3507841B2 (en) Steam or hot water heating device
JP4330730B2 (en) Steam heating device
JP4387536B2 (en) Steam heating device
JP4409715B2 (en) Steam heating device
JP2002122389A (en) Steam heater
JPH06300205A (en) Steam heating apparatus
JP2000356306A (en) Steam heater
JP2665838B2 (en) Heating and cooling device
JP5047426B2 (en) Steam heating device
JP4472102B2 (en) Steam heating device
GB2198055A (en) Air conditioning system
JP3537206B2 (en) Steam heating device
JPH0366580B2 (en)
JP4545560B2 (en) Steam heating device
JPS6259601B2 (en)
JP5047425B2 (en) Steam heating device
JPH08168668A (en) Vapor heater

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

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

Free format text: PAYMENT UNTIL: 20090301

Year of fee payment: 7

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

Year of fee payment: 8

Free format text: PAYMENT UNTIL: 20100301

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

Free format text: PAYMENT UNTIL: 20110301

Year of fee payment: 9

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

Free format text: PAYMENT UNTIL: 20130301

Year of fee payment: 11

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

Year of fee payment: 12

Free format text: PAYMENT UNTIL: 20140301

LAPS Cancellation because of no payment of annual fees