JP2554956B2 - Steam heating and evaporative cooling equipment - Google Patents

Steam heating and evaporative cooling equipment

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Publication number
JP2554956B2
JP2554956B2 JP2310606A JP31060690A JP2554956B2 JP 2554956 B2 JP2554956 B2 JP 2554956B2 JP 2310606 A JP2310606 A JP 2310606A JP 31060690 A JP31060690 A JP 31060690A JP 2554956 B2 JP2554956 B2 JP 2554956B2
Authority
JP
Japan
Prior art keywords
cooling
heating
supply pipe
steam
fluid chamber
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.)
Expired - Fee Related
Application number
JP2310606A
Other languages
Japanese (ja)
Other versions
JPH04180829A (en
Inventor
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 JP2310606A priority Critical patent/JP2554956B2/en
Publication of JPH04180829A publication Critical patent/JPH04180829A/en
Application granted granted Critical
Publication of JP2554956B2 publication Critical patent/JP2554956B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 <産業上の利用分野> 本発明は加熱と冷却を行う加熱冷却装置に関し、特
に、比較的低い温度での上記加熱及び減圧気化冷却を行
う蒸気加熱及び気化冷却装置に関する。蒸気の加熱冷却
装置としては、各種合成樹脂やアセトン等の溶剤の製造
工程における重合反応に用いられる反応釜等がある。
Description: TECHNICAL FIELD The present invention relates to a heating / cooling device for heating and cooling, and more particularly to a steam heating / vaporization cooling device for performing the above heating at a relatively low temperature and reduced pressure evaporative cooling. . As a heating and cooling device for steam, there is a reaction vessel or the like used for a polymerization reaction in the production process of various synthetic resins and solvents such as acetone.

<従来の技術> 従来の加熱冷却装置として、第2図に示す反応釜の加
熱冷却装置がある。図において、1は反応釜であり、原
料入口2、製品出口3、撹拌機4、ジャケット部5を有
している。ジャケット部5には加熱及び冷却のための流
体給排口6,7を設けてあり、その一方には冷却水供給管
8及び復水排出管9を接続し、他方には蒸気供給管10及
び冷却水排出管11を接続し、各管の途中に弁V1、V2、V
3、V4を設けてある。この反応釜1内の原料を加熱する
場合は、弁V2、V4を閉じ、弁V1、V3を開く。これによっ
て蒸気が管10、流体給排口7からジャケット部5内に供
給されて加熱が行なわれ、復水排出管9を通りスチーム
トラップ12を経て排出される。
<Prior Art> As a conventional heating / cooling apparatus, there is a heating / cooling apparatus for a reaction kettle shown in FIG. In the figure, reference numeral 1 denotes a reaction vessel, which has a raw material inlet 2, a product outlet 3, a stirrer 4, and a jacket portion 5. The jacket 5 is provided with fluid supply / discharge ports 6 and 7 for heating and cooling, one of which is connected to a cooling water supply pipe 8 and a condensate discharge pipe 9, and the other is connected to a steam supply pipe 10 and Connect the cooling water discharge pipe 11 and insert valves V1, V2, V in the middle of each pipe.
3 and V4 are provided. When heating the raw material in the reaction kettle 1, the valves V2 and V4 are closed and the valves V1 and V3 are opened. As a result, steam is supplied from the pipe 10 and the fluid supply / discharge port 7 into the jacket portion 5 for heating, and then discharged through the condensate discharge pipe 9 and the steam trap 12.

また冷却する場合は、弁V1、V3を閉じ、弁V2、V4を開
く。これによって冷却水が管8、流体給排口6を通って
ジャケット部5内に供給されて冷却が行なわれる。供給
された冷却水は流体給排口7、管11を通って排出され
る。
For cooling, valves V1 and V3 are closed and valves V2 and V4 are opened. As a result, cooling water is supplied into the jacket portion 5 through the pipe 8 and the fluid supply / discharge port 6, and cooling is performed. The supplied cooling water is discharged through the fluid supply / discharge port 7 and the pipe 11.

<発明が解決しようとする課題> 上記従来の加熱冷却装置は、加熱時において直接蒸気
を供給すると供給熱量が多すぎて被加熱物を損傷する問
題、及び、冷却時において、反応釜を均一に冷却でき
ず、部分的な異常昇温が発生し、この温度ムラによって
製品の品質を一定に維持し難い問題があった。供給熱量
を低減するためには温水加熱を行うこともできるが、温
水の場合、通常加熱温度が100℃以下と限定されると共
に温水を製造するための設備を新たに設置しなければな
らない。又、冷却時における温度ムラの原因は、冷却水
による冷却であるため、水の顕熱のみによる冷却となり
熱容量が小さいためである。
<Problems to be Solved by the Invention> The conventional heating / cooling device described above has a problem that when the steam is directly supplied during heating, the amount of heat supplied is too large to damage the object to be heated, and during cooling, the reaction vessel is made uniform. There was a problem that it was difficult to keep the quality of the product constant due to the temperature unevenness because the temperature could not be cooled and a partial abnormal temperature rise occurred. In order to reduce the amount of heat supplied, hot water heating can be performed, but in the case of hot water, the heating temperature is usually limited to 100 ° C or lower, and equipment for producing hot water must be newly installed. Further, the cause of the temperature unevenness during cooling is that the cooling is performed by the cooling water, so that the cooling is performed only by the sensible heat of the water and the heat capacity is small.

従って本発明の技術的課題は、加熱冷却装置におい
て、加熱時の蒸気の供給熱量を適度に押えて被加熱物の
損傷を防止すると共に、冷却時の熱容量を大きくするこ
とにより冷却の温度ムラを無くして製品の品質を一定に
維持することである。
Therefore, the technical problem of the present invention, in the heating and cooling device, while preventing the damage of the object to be heated by appropriately pressing the supply heat amount of the steam during heating, while increasing the heat capacity during cooling, uneven temperature of cooling. It is to maintain the quality of the product by eliminating it.

<課題を解決する為の手段> 上記課題を解決するために講じた本発明の技術的手段
は、被加熱冷却容器に接して加熱及び冷却用流体室を形
成し、該流体室へ加熱時に弁装置を介して蒸気を供給す
る蒸気供給管を接続し、冷却時に弁装置を介して冷却水
を供給する冷却水供給管を接続すると共に流体室を真空
ポンプと接続したものにおいて、流体室内で上記被加熱
冷却容器の外壁を覆うように隙間を介して気液分離機能
高分子膜を設け、当該気液分離機能高分子膜の外周側に
蒸気供給管と真空ポンプを接続し、内周側に冷却水供給
管を接続して、気液分離機能高分子膜の下端部に貫通孔
を設けたものである。
<Means for Solving the Problem> The technical means of the present invention taken to solve the above-mentioned problems is to form a heating and cooling fluid chamber in contact with a heated and cooled container, and to apply a valve to the fluid chamber when heating. A steam supply pipe for supplying steam through the device is connected, a cooling water supply pipe for supplying cooling water is connected through a valve device at the time of cooling, and a fluid chamber is connected to a vacuum pump. A gas-liquid separation functional polymer film is provided through a gap so as to cover the outer wall of the heated cooling container, the vapor supply pipe and the vacuum pump are connected to the outer peripheral side of the gas-liquid separation functional polymer film, and the inner peripheral side is connected. A cooling water supply pipe is connected and a through hole is provided at the lower end of the gas-liquid separation functional polymer membrane.

<作 用> 加熱する場合は、弁装置を経て加熱蒸気を流体室に供
給する蒸気供給管を開く。流体室に至った蒸気は、気液
分離機能高分子膜を介して被加熱容器と接することによ
り、気液分離機能高分子膜が蒸気通貨の抵抗となり、供
給熱量が適度に押えられ、気液分離機能高分子膜の下端
部に設けられた貫通孔を経て流入してきた蒸気と共に被
加熱容器を加熱する。被加熱容器を加熱して復水化した
ドレンは、気液分離機能高分子膜と被加熱容器との間の
隙間を通り下方へ滴下し、気液分離機能高分子膜下端部
に設けた貫通孔を経て流体室に至り真空ポンプによって
系外に排除される。
<Operation> When heating, open the steam supply pipe that supplies heated steam to the fluid chamber through the valve device. The vapor that reaches the fluid chamber comes into contact with the container to be heated via the gas-liquid separation function polymer film, and the gas-liquid separation function polymer film becomes the resistance of the steam currency, and the supplied heat amount is appropriately suppressed, The heated container is heated together with the vapor that has flowed in through the through hole provided at the lower end of the separation functional polymer membrane. The condensate drained by heating the heated container is dripped downward through the gap between the gas-liquid separating polymer film and the heated container, and penetrates through the bottom end of the gas-liquid separating polymer film. It reaches the fluid chamber through the hole and is removed from the system by the vacuum pump.

冷却する場合は、蒸気供給管を閉じ、冷却水供給管の
弁装置を開弁して、冷却水を流体室に供給すると共に真
空ポンプで流体室内を減圧する。冷却水は被冷却容器と
気液分離機能高分子膜の隙間に至り、被冷却容器外周の
全面に均一に付着し、被冷却物の熱及び減圧状態である
がために速やかに気化して被冷却物を気化冷却する。気
化した蒸気は気液分離機能高分子膜の一部を通過して流
体室に至り真空ポンプによって系外に排除される。
In the case of cooling, the steam supply pipe is closed, the valve device of the cooling water supply pipe is opened, the cooling water is supplied to the fluid chamber, and the pressure inside the fluid chamber is reduced by the vacuum pump. The cooling water reaches the gap between the container to be cooled and the polymer film for gas-liquid separation function, uniformly adheres to the entire outer circumference of the container to be cooled, and is rapidly vaporized due to the heat and reduced pressure of the object to be cooled. Evaporative cooling of the cooled product. The vaporized vapor passes through a part of the gas-liquid separation functional polymer membrane, reaches the fluid chamber, and is removed from the system by a vacuum pump.

<実施例> 上記技術的手段の具体例を示す実施例を説明する。
(第1図参照) 本実施例においては、加熱冷却装置として反応釜を用
いた例を示す。
<Example> An example showing a specific example of the above technical means will be described.
(See FIG. 1) In this embodiment, an example in which a reaction kettle is used as a heating / cooling device is shown.

第1図において、21は反応釜、22はポンプ装置、23は
弁装置、24は水温制御部、25は余剰水排出手段、26は弁
装置、27は蒸気供給管、28は冷却水供給管である。
In FIG. 1, 21 is a reaction vessel, 22 is a pump device, 23 is a valve device, 24 is a water temperature control unit, 25 is excess water discharge means, 26 is a valve device, 27 is a steam supply pipe, 28 is a cooling water supply pipe. Is.

反応釜21は、原料入口2、製品出口3、撹拌機4、蒸
気加熱及び気化冷却用の流体室としてのジャケット部5
を有しており、ジャケット部5には流体排出口7を設け
てある。蒸気供給管27と冷却水供給管28はそれぞれ弁装
置23,26を介してジャケット部5と接続する。ジャケッ
ト部5内に、反応釜21の外周を覆うように、気液分離機
能高分子膜20を設ける。気液分離機能高分子膜20と反応
釜21の外周との間には隙間を設ける。蒸気供給管27はジ
ャケット部5において気液分離機能高分子膜20の外周と
接続し、冷却水供給管28は気液分離機能高分子膜20の内
周と接続せしめる。気液分離機能高分子膜20の下端部で
製品出口3の周囲に貫通孔16を設ける。
The reaction vessel 21 includes a raw material inlet 2, a product outlet 3, a stirrer 4, and a jacket portion 5 as a fluid chamber for steam heating and evaporative cooling.
The jacket portion 5 is provided with a fluid discharge port 7. The steam supply pipe 27 and the cooling water supply pipe 28 are connected to the jacket portion 5 via valve devices 23 and 26, respectively. A gas-liquid separation functional polymer membrane 20 is provided in the jacket 5 so as to cover the outer periphery of the reaction vessel 21. A gap is provided between the gas-liquid separation functional polymer membrane 20 and the outer periphery of the reaction vessel 21. The steam supply pipe 27 is connected to the outer periphery of the gas-liquid separation functional polymer film 20 in the jacket portion 5, and the cooling water supply pipe 28 is connected to the inner periphery of the gas-liquid separation functional polymer film 20. A through hole 16 is provided around the product outlet 3 at the lower end of the gas-liquid separation functional polymer membrane 20.

ポンプ装置22は、ポンプ30がタンク31に吸込側を接続
され吐出側をエゼクタ32のノズル33に接続し、エゼクタ
32のディフューザ34がタンク31の上部空間に接続された
構成のものであり、エゼクタ32と流体排出口7とが接続
されている。このポンプ装置22は、ポンプ30の作動によ
りタンク31内の水をエゼクタ32に供給して吸引作用さ
せ、タンク31に戻すようになっている。
In the pump device 22, the pump 30 has the suction side connected to the tank 31 and the discharge side connected to the nozzle 33 of the ejector 32,
The diffuser 34 of 32 is connected to the upper space of the tank 31, and the ejector 32 and the fluid discharge port 7 are connected to each other. The pump device 22 is configured to supply the water in the tank 31 to the ejector 32 by the operation of the pump 30 to cause the ejector 32 to suck the water, and to return the water to the tank 31.

弁装置26は、冷却水供給通路28に取付けて、ポンプ30
の吐出水の一部をジャケット部5に供給あるいは遮断す
る電動弁で、コントロール部29からの信号により開閉動
作する。
The valve device 26 is attached to the cooling water supply passage 28, and the pump 30
This is an electrically operated valve that supplies or shuts off a part of the discharge water of the jacket 5 and is opened / closed by a signal from the controller 29.

水温制御部24は、タンク31内の水温を制御するように
設けたものであり、タンク31内に冷却水を供給すること
によって制御するようになっている。タンク31に接続し
た冷却水供給管40の途中に電動弁70を設け、タンク内の
水温を検出する温度センサー41からの信号により開閉す
る。
The water temperature control unit 24 is provided to control the water temperature in the tank 31, and is controlled by supplying cooling water into the tank 31. An electric valve 70 is provided in the middle of the cooling water supply pipe 40 connected to the tank 31, and is opened / closed by a signal from a temperature sensor 41 that detects the water temperature in the tank.

余剰水排出手段25は、ポンプ装置22の一部に電動弁71
を取付け、タンク31内の水位センサー42a,42bからの信
号により、タンク31内の水位を所定範囲に保つものであ
る。
The surplus water discharging means 25 includes a motorized valve 71 in a part of the pump device 22.
Is attached and the water level in the tank 31 is kept within a predetermined range by signals from the water level sensors 42a and 42b in the tank 31.

弁装置26以外の電動弁70,71,及び弁装置23もコントロ
ール部29と接続して集中制御できるようにする。
The motor-operated valves 70 and 71 other than the valve device 26 and the valve device 23 are also connected to the control unit 29 so that centralized control is possible.

反応釜21を加熱する場合は、コントロール部29からの
信号により、弁装置23が開き蒸気がジャケット部5に供
給され、反応釜21を蒸気加熱する。この場合、供給され
た蒸気は気液分離機能高分子膜20により、反応釜21と接
触する量が制限され、被加熱物としての原料が熱損傷す
ることを防止する。加熱により生じたドレンは、下端の
貫通孔16を経て、エゼクタ32に吸引されタンク31に至
る。ドレンによってタンク31内の水位が上限水位に達す
ると、水位センサー42aが検知し、電動弁71が開き、余
剰水を系外に排出する。
When the reaction kettle 21 is heated, the valve device 23 is opened by the signal from the control unit 29 and steam is supplied to the jacket portion 5 to heat the reaction kettle 21 with steam. In this case, the supplied vapor limits the amount of contact with the reaction vessel 21 by the gas-liquid separation functional polymer membrane 20, and prevents the raw material as the article to be heated from being thermally damaged. The drain generated by heating is sucked by the ejector 32 and reaches the tank 31 through the through hole 16 at the lower end. When the water level in the tank 31 reaches the upper limit water level by the drain, the water level sensor 42a detects it, the electric valve 71 opens, and the surplus water is discharged to the outside of the system.

冷却する場合は、弁装置23を閉じて蒸気の供給を停止
し、弁装置26を開弁し、ポンプ30からの吐出水の一部を
ジャケット部5に供給する。供給された冷却水は気液分
離機能高分子膜20により、反応釜21の外壁全体に均一に
付着する。エゼクタ32に生じる吸引作用すなわち減圧作
用により、ジャケット部5内も減圧される。ジャケット
部5内が減圧されると、均一に付着した冷却水は反応釜
21の熱により迅速に気化して原料を冷却する。
In the case of cooling, the valve device 23 is closed to stop the supply of steam, the valve device 26 is opened, and a part of the water discharged from the pump 30 is supplied to the jacket part 5. The supplied cooling water is uniformly attached to the entire outer wall of the reaction vessel 21 by the gas-liquid separation functional polymer film 20. The inside of the jacket portion 5 is also depressurized by the suction action, that is, the depressurizing action generated in the ejector 32. When the inside of the jacket 5 is decompressed, the cooling water that has uniformly adhered to the reaction vessel
The heat of 21 rapidly vaporizes and cools the raw material.

ジャケット部5内の減圧度は、タンク31の水温を調整
することにより制御することができる。
The degree of pressure reduction in the jacket portion 5 can be controlled by adjusting the water temperature of the tank 31.

<発明の効果> 本発明によれば、加熱時に適度な熱量を供給すること
がなく、被加熱物を熱損傷することがない。また、冷却
時においても被冷却容器全体に均一な冷却水を供給し、
冷却室を減圧して気化冷却するから均一且つ大きな熱容
量で冷却することができ、冷却ムラを防止して、製品の
品質を一定に維持できる。
<Effects of the Invention> According to the present invention, an appropriate amount of heat is not supplied during heating, and the object to be heated is not thermally damaged. In addition, even during cooling, uniform cooling water is supplied to the entire container to be cooled,
Since the cooling chamber is depressurized and vaporized to be cooled, it can be cooled uniformly and with a large heat capacity, and it is possible to prevent uneven cooling and maintain a constant product quality.

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

第1図は本発明の蒸気加熱及び気化冷却装置の実施例の
概略の構成を示す構成図、第2図は従来の加熱冷却装置
の一例を示す概略構成図である。 5:ジャケット部、7:流体排出口 16:貫通孔、20:気液分離機能高分子膜 21:反応釜、22:ポンプ装置 27:蒸気供給管、28:冷却水供給管 31:タンク、32:エゼクタ
FIG. 1 is a schematic diagram showing a schematic configuration of an embodiment of a steam heating and evaporative cooling device of the present invention, and FIG. 2 is a schematic configuration diagram showing an example of a conventional heating and cooling device. 5: Jacket part, 7: Fluid discharge port 16: Through hole, 20: Polymer membrane with gas-liquid separation function 21: Reactor, 22: Pump device 27: Steam supply pipe, 28: Cooling water supply pipe 31: Tank, 32 : Ejector

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】被加熱冷却容器に接して加熱及び冷却用流
体室を形成し、該流体室へ加熱時に弁装置を介して蒸気
を供給する蒸気供給管を接続し、冷却時に弁装置を介し
て冷却水を供給する冷却水供給管を接続すると共に流体
室を真空ポンプと接続したものにおいて、流体室内で上
記被加熱冷却容器の外壁を覆うように隙間を介して気液
分離機能高分子膜を設け、当該気液分離機能高分子膜の
外周側に蒸気供給管と真空ポンプを接続し、内周側に冷
却水供給管を接続して、気液分離機能高分子膜の下端部
に貫通孔を設けたことを特徴とする蒸気加熱及び気化冷
却装置。
1. A heating and cooling fluid chamber is formed in contact with a heated cooling container, a steam supply pipe for supplying steam to the fluid chamber via a valve device at the time of heating is connected to the fluid chamber, and a valve device is connected at the time of cooling. A cooling water supply pipe for supplying cooling water and a fluid chamber connected to a vacuum pump, wherein a gas-liquid separation functional polymer film is provided in the fluid chamber through a gap so as to cover the outer wall of the heated cooling container. A vapor supply pipe and a vacuum pump are connected to the outer peripheral side of the gas-liquid separation functional polymer membrane, a cooling water supply pipe is connected to the inner peripheral side, and the lower end of the gas-liquid separation functional polymer membrane is penetrated. A steam heating and evaporative cooling device having holes.
JP2310606A 1990-11-15 1990-11-15 Steam heating and evaporative cooling equipment Expired - Fee Related JP2554956B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2310606A JP2554956B2 (en) 1990-11-15 1990-11-15 Steam heating and evaporative cooling equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2310606A JP2554956B2 (en) 1990-11-15 1990-11-15 Steam heating and evaporative cooling equipment

Publications (2)

Publication Number Publication Date
JPH04180829A JPH04180829A (en) 1992-06-29
JP2554956B2 true JP2554956B2 (en) 1996-11-20

Family

ID=18007285

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2310606A Expired - Fee Related JP2554956B2 (en) 1990-11-15 1990-11-15 Steam heating and evaporative cooling equipment

Country Status (1)

Country Link
JP (1) JP2554956B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6739288B1 (en) 2000-01-14 2004-05-25 Tvl Co., Ltd. Steam heating device
JP2008045787A (en) * 2006-08-11 2008-02-28 Tlv Co Ltd Evaporative cooling device
JP2010266143A (en) * 2009-05-15 2010-11-25 Tlv Co Ltd Vaporization cooling device

Also Published As

Publication number Publication date
JPH04180829A (en) 1992-06-29

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