JPH0566502B2 - - Google Patents

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Publication number
JPH0566502B2
JPH0566502B2 JP60283562A JP28356285A JPH0566502B2 JP H0566502 B2 JPH0566502 B2 JP H0566502B2 JP 60283562 A JP60283562 A JP 60283562A JP 28356285 A JP28356285 A JP 28356285A JP H0566502 B2 JPH0566502 B2 JP H0566502B2
Authority
JP
Japan
Prior art keywords
liquid
gas
refrigerant
receiver
liquid receiver
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
JP60283562A
Other languages
Japanese (ja)
Other versions
JPS62142964A (en
Inventor
Tatsunori Otake
Masao Noguchi
Takeji Watanabe
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP28356285A priority Critical patent/JPS62142964A/en
Publication of JPS62142964A publication Critical patent/JPS62142964A/en
Publication of JPH0566502B2 publication Critical patent/JPH0566502B2/ja
Granted legal-status Critical Current

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  • Central Heating Systems (AREA)
  • Yarns And Mechanical Finishing Of Yarns Or Ropes (AREA)
  • General Preparation And Processing Of Foods (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明はヒートポンプ式暖房装置の性能向上に
関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to improving the performance of a heat pump type heating device.

従来の技術 従来のヒートポンプ式暖房装置は外気温度が低
下するにつれて冷媒の蒸発温度が低下し、その結
果、凝縮器への冷媒循環量が減少し暖房能力が低
下するという欠点があつた。この暖房能力の低下
を補うため第2図に示すように圧縮機1、凝縮器
2、減圧装置3、蒸発器4からなる暖房主循環回
路の液化冷媒を第1逆止弁6を介し受液器5へ送
り、制御開閉弁7の開閉により、すなわち制御開
閉弁7が開のときは前記受液器5へ溜つている液
冷媒を第2逆止弁8を通つて加熱器9へ重力によ
り供給し、このときは前記受液器5と加熱器9と
は均圧されているため第1逆止弁6により受液器
5へは暖房主循環回路から液冷媒は流入せず、受
液器5の液冷媒がなくなると前記制御開閉弁7を
閉じ、受液器5へ暖房主循環回路から液冷媒を第
1逆止弁6を通つて流入させ(このとき加熱器圧
力は受液器圧力より高いので受液器5への流入液
冷媒は第2逆止弁8により加熱器9へは流れ込ま
ない。)受液器5へ液冷媒が溜ると再び制御開閉
弁7を開にし加熱器9へ液冷媒を供給する。すな
わち加熱器9へは受液器5から間欠的に液冷媒が
供給され、加熱器9で吸熱蒸発した冷媒ガスは圧
縮機1の吐出ガスと共に凝縮器2へ送られ低外気
温時における凝縮能力低下の防止を図つている。
(例えば特開昭60−89627号公報) 発明が解決しようとする問題点 しかしながら第2図のような構成では、受液器
5に溜つた液冷媒を加熱器9へ供給する際、開状
態の制御開閉弁7を通つて加熱器9で吸熱ガス化
した冷媒が受液器5へ流入して受液器5の温度が
上昇し、制御開閉弁7の閉時暖房主循環回路から
第1逆止弁6を通つて受液器5へ液冷媒を流入さ
せる時、受液器5のガス部容積が液部の増加によ
り圧縮されて、受液器5への液冷媒流入量が減少
し、その結果加熱器9の液冷媒量が不足し加熱器
9内の冷媒ガス温度が上昇し、冷媒の熱安定性が
損われるという問題点を有していた。またさらに
暖房主循環回路の凝縮器2出口の液冷媒を円滑に
受液器5へ流入させるために前記受液器5のガス
冷媒を暖房主循環回路の低圧側へ逃がしてやる方
法もあるが(例えば特開昭60−93237号公報)冷
媒回路が複雑になる問題点を有していた。
BACKGROUND ART Conventional heat pump heating devices have had the disadvantage that as the outside air temperature decreases, the evaporation temperature of the refrigerant decreases, resulting in a decrease in the amount of refrigerant circulated to the condenser and a decrease in heating capacity. In order to compensate for this decrease in heating capacity, as shown in FIG. By opening and closing the control valve 7, that is, when the control valve 7 is open, the liquid refrigerant accumulated in the liquid receiver 5 is sent to the heater 9 through the second check valve 8 by gravity. At this time, since the liquid receiver 5 and the heater 9 are pressure-equalized, the first check valve 6 prevents liquid refrigerant from flowing into the liquid receiver 5 from the heating main circulation circuit. When the liquid refrigerant in the heater 5 runs out, the control on-off valve 7 is closed, and the liquid refrigerant flows into the receiver 5 from the heating main circulation circuit through the first check valve 6 (at this time, the heater pressure is equal to (Since the liquid refrigerant flowing into the liquid receiver 5 is higher than the pressure, it does not flow into the heater 9 by the second check valve 8.) When the liquid refrigerant accumulates in the liquid receiver 5, the control opening/closing valve 7 is opened again and the heater is turned off. Supply liquid refrigerant to 9. In other words, the liquid refrigerant is intermittently supplied to the heater 9 from the liquid receiver 5, and the refrigerant gas that has absorbed heat and evaporated in the heater 9 is sent to the condenser 2 together with the discharge gas of the compressor 1 to improve the condensation capacity at low outside temperatures. Efforts are being made to prevent this decline.
(For example, Japanese Unexamined Patent Publication No. 60-89627) Problems to be Solved by the Invention However, in the configuration shown in FIG. The refrigerant that has been endothermically gasified by the heater 9 flows through the control on-off valve 7 into the liquid receiver 5, and the temperature of the liquid receiver 5 rises. When the liquid refrigerant flows into the liquid receiver 5 through the stop valve 6, the gas portion volume of the liquid receiver 5 is compressed due to the increase in the liquid portion, and the amount of liquid refrigerant flowing into the liquid receiver 5 decreases. As a result, there was a problem in that the amount of liquid refrigerant in the heater 9 was insufficient, the temperature of the refrigerant gas in the heater 9 increased, and the thermal stability of the refrigerant was impaired. Furthermore, in order to smoothly flow the liquid refrigerant at the outlet of the condenser 2 of the heating main circulation circuit into the liquid receiver 5, there is a method in which the gas refrigerant in the liquid receiver 5 is released to the low pressure side of the heating main circulation circuit. (For example, Japanese Patent Application Laid-Open No. 60-93237) had the problem that the refrigerant circuit was complicated.

本発明はかかる従来の問題点を解決するもの
で、機器の信頼性向上をはかると共に機器のコン
パクト化をはかる目的のものである。
The present invention is intended to solve these conventional problems, and aims to improve the reliability of the device and make the device more compact.

問題点を解決するための手段 上記問題点を解決するために本発明の暖房装置
は、圧縮機、アキユムレータ、凝縮器、減圧装
置、蒸発器とからなるヒートポンプサイクルと、
前記ヒートポンプサイクルの高圧液部から第1逆
止弁を介し連結した受液器、前記受液器の下方に
第2逆止弁を介して連結した気液分離器、前記気
液分離器からガス戻し管を前記圧縮機の吐出管
と、開閉弁を有する均圧管を前記受液器と各々連
結すると共に前記気液分離器の液管と戻り管を冷
媒加熱器と連結したサイクルとからなり、仕切り
板により2つの空間を形成する容器の一方を前記
アキユムレータ、他方を前記受液器とし、アキユ
ムレータと受液器とを一体化構成としたものであ
る。
Means for Solving the Problems In order to solve the above problems, the heating device of the present invention includes a heat pump cycle consisting of a compressor, an accumulator, a condenser, a pressure reducing device, and an evaporator;
A liquid receiver connected to the high-pressure liquid part of the heat pump cycle via a first check valve; a gas-liquid separator connected below the liquid receiver via a second check valve; a cycle in which a return pipe is connected to a discharge pipe of the compressor, a pressure equalizing pipe having an on-off valve is connected to the liquid receiver, and a liquid pipe and a return pipe of the gas-liquid separator are connected to a refrigerant heater; One of the containers forming two spaces by a partition plate is the accumulator, and the other is the liquid receiver, and the accumulator and the liquid receiver are integrated.

作 用 本発明は上記した構成によつて受液器はヒート
ポンプサイクルの低圧部であるアキユムレータと
仕切り板を介して一体化構成としてあるので伝熱
効果により開閉弁が開時気液分離器から流入して
きたガス冷媒を凝縮させ、開閉弁が閉時、ヒート
ポンプサイクル側の高圧液冷媒が受液器へ流入す
ることが円滑に行なわれる作用があり、その結果
気液分離器には受液器から液冷媒が不足すること
なく供給され冷媒加熱器へ供給される液冷媒も不
足することはないから冷媒が熱分解することなく
サイクルの信頼性の向上、機器のコンパクト化が
得られる。
Effects In the present invention, the liquid receiver is integrated with the accumulator, which is the low-pressure part of the heat pump cycle, through the partition plate. When the on-off valve closes, the high-pressure liquid refrigerant on the heat pump cycle side smoothly flows into the liquid receiver, and as a result, the gas-liquid separator has the effect of condensing the gas refrigerant from the liquid receiver. Since there is no shortage of liquid refrigerant and there is no shortage of liquid refrigerant supplied to the refrigerant heater, the refrigerant does not undergo thermal decomposition, improving cycle reliability and making equipment more compact.

実施例 以下、本発明の実施例を添付図面にもとづいて
説明する。
Embodiments Hereinafter, embodiments of the present invention will be described based on the accompanying drawings.

第1図において、10は圧縮機、11は凝縮
器、12は減圧装置、13は蒸発器、14は仕切
り板、16により受液器15と一体化構成となつ
ているアキユムレータで、ヒートポンプサイクル
を構成している。17は前記受液器15とヒート
ポンプサイクル高圧液部とを接続する管に配設し
てある第1逆止弁、18は前記受液器15の下方
に配設してある気液分離器で、前記受液器15と
は第2逆止弁19を介して接続されている。20
は前記気液分離器18と前記圧縮機1の吐出管と
を接続するガス戻し管、21は前記気液分離器1
8と受液器15とを連結する均圧管22に配設し
てある開閉弁、23,24はそれぞれ前記気液分
離器18に配設してある液管と戻り管で冷媒加熱
器25と連結している。
In FIG. 1, 10 is a compressor, 11 is a condenser, 12 is a pressure reducing device, 13 is an evaporator, 14 is a partition plate, and 16 is an accumulator that is integrated with a liquid receiver 15, and a heat pump cycle is performed. It consists of 17 is a first check valve installed in a pipe connecting the liquid receiver 15 and the high-pressure liquid section of the heat pump cycle; 18 is a gas-liquid separator installed below the liquid receiver 15; , and is connected to the liquid receiver 15 via a second check valve 19. 20
21 is a gas return pipe connecting the gas-liquid separator 18 and the discharge pipe of the compressor 1, and 21 is the gas-liquid separator 1.
Opening/closing valves 23 and 24 are installed in the pressure equalizing pipe 22 that connects the liquid receiver 15 and the liquid receiver 15. It is connected.

上記構成において圧縮機10で高温高圧になつ
た冷媒は凝縮器11で凝縮液化し減圧装置12で
減圧膨張し蒸発器13でガス化したアキユムレー
タ14をへて圧縮機9へ戻る。一方、前記ヒート
ポンプサイクルの高圧液部から分流した液冷媒は
開閉弁21が閉のとき第1逆止弁17を通つて受
液器15へ溜る。このとき気液分離器18の圧力
は受液器15の圧力よりも高いため第2逆止弁1
9により受液器15に流入する液冷媒は気液分離
器18へ流れ込まない。次に受液器15の液冷媒
が溜り込むと開閉弁21を開とし受液器15の圧
力は気液分離器18の圧力と均圧管22により等
しくなり、気液分離器18は受液器15より下方
に配設してあるため重力により受液器15に溜つ
ていた液冷媒は気液分離器18へ流入する。この
とき受液器15の圧力は気液分離器18の圧力と
等しいため第1逆止弁17は閉となりヒートポン
プサイクル高圧液部から受液器15へ液冷媒は流
入しない。気液分離器18へ流入した液冷媒は自
然循環で液管23から冷媒加熱器25へ流入し吸
熱蒸発し二相状態で戻り管24を通り再び気液分
離器18へ戻りガス冷媒のみがガス戻し管20を
通つて圧縮機10の吐出ガスと合流し凝縮器11
へ流入する。又、二相状態で戻り管24を通り気
液分離器18へ戻つてきた液冷媒は再び冷媒加熱
器25へ流入する。以上のように開閉弁21の開
閉により受液器15へヒートポンプサイクル高圧
液部から溜り込んだ液冷媒を間欠的に気液分離器
18へ供給してやり気液分離器18と冷媒加熱器
25の二相自然循環サイクルを行なわせることに
より連続的に冷媒加熱器25で吸熱蒸発したガス
冷媒を圧縮機1の吐出ガスと合流させ凝縮器2へ
搬送するものである。ここで冷媒加熱器25から
の吸熱を冷媒が熱分解することなく二相状態で行
なわせるためには受液器15に円滑に液冷媒を溜
め込むことが必要であるが本実施例ではヒートポ
ンプサイクルの低圧側であるアキユムレータ14
と仕切り板16を介して受液器15を一体化して
あるため、開閉弁21が開時、気液分離器18か
ら均圧管22を通つて流入するガス冷媒がアキユ
ムレータ14の低温部に接し凝縮し、開閉弁21
が閉時高圧液冷媒が受液器15流入時ガス部容積
を圧縮することがなく、円滑に受液器15へヒー
トポンプサイクル側から液冷媒が溜り込む。した
がつて受液器15から気液分離器18への冷媒供
給量も不足することなくその結果冷媒加熱器25
での冷媒の熱分解が防止できサイクルの信頼性が
向上すると共に機器のコンパクト化が可能となる
効果がある。
In the above configuration, the refrigerant that has become high temperature and high pressure in the compressor 10 is condensed and liquefied in the condenser 11, expanded under reduced pressure in the pressure reducing device 12, gasified in the evaporator 13, and returned to the compressor 9 through the accumulator 14. On the other hand, the liquid refrigerant separated from the high-pressure liquid part of the heat pump cycle passes through the first check valve 17 and accumulates in the liquid receiver 15 when the on-off valve 21 is closed. At this time, the pressure in the gas-liquid separator 18 is higher than the pressure in the liquid receiver 15, so the second check valve 1
9 prevents the liquid refrigerant flowing into the liquid receiver 15 from flowing into the gas-liquid separator 18. Next, when the liquid refrigerant in the liquid receiver 15 accumulates, the on-off valve 21 is opened and the pressure in the liquid receiver 15 becomes equal to the pressure in the gas-liquid separator 18 through the pressure equalization pipe 22, and the gas-liquid separator 18 Since the liquid refrigerant is disposed below the liquid receiver 15, the liquid refrigerant accumulated in the liquid receiver 15 flows into the gas-liquid separator 18 due to gravity. At this time, the pressure in the liquid receiver 15 is equal to the pressure in the gas-liquid separator 18, so the first check valve 17 is closed, and liquid refrigerant does not flow into the liquid receiver 15 from the high-pressure liquid section of the heat pump cycle. The liquid refrigerant that has flowed into the gas-liquid separator 18 flows through the liquid pipe 23 into the refrigerant heater 25 through natural circulation, absorbs heat, evaporates, passes through the return pipe 24 in a two-phase state, returns to the gas-liquid separator 18, and only the gas refrigerant becomes a gas. It passes through the return pipe 20 and joins the discharge gas of the compressor 10 to the condenser 11
flow into. Further, the liquid refrigerant that has returned to the gas-liquid separator 18 through the return pipe 24 in a two-phase state flows into the refrigerant heater 25 again. As described above, by opening and closing the on-off valve 21, the liquid refrigerant accumulated in the liquid receiver 15 from the high-pressure liquid section of the heat pump cycle is intermittently supplied to the gas-liquid separator 18. By performing a phase natural circulation cycle, the gas refrigerant that has been continuously endothermically evaporated in the refrigerant heater 25 is combined with the discharge gas of the compressor 1 and conveyed to the condenser 2. Here, in order to absorb heat from the refrigerant heater 25 in a two-phase state without thermal decomposition of the refrigerant, it is necessary to smoothly store the liquid refrigerant in the liquid receiver 15, but in this embodiment, the heat pump cycle Accumulator 14 on the low pressure side
Since the liquid receiver 15 is integrated with the liquid receiver 15 via the partition plate 16, when the on-off valve 21 is opened, the gas refrigerant flowing from the gas-liquid separator 18 through the pressure equalization pipe 22 comes into contact with the low temperature part of the accumulator 14 and condenses. On-off valve 21
When closed, the high-pressure liquid refrigerant flows into the liquid receiver 15 without compressing the gas section volume, and the liquid refrigerant smoothly accumulates in the liquid receiver 15 from the heat pump cycle side. Therefore, the amount of refrigerant supplied from the liquid receiver 15 to the gas-liquid separator 18 is not insufficient, and as a result, the refrigerant heater 25
This has the effect of preventing thermal decomposition of the refrigerant in the air, improving cycle reliability and making equipment more compact.

発明の効果 以上のように本発明の暖房装置によれば、ヒー
トポンプサイクルのアキユムレーターと受液器と
を一体化してあるため気液分離器へ受液器から液
冷媒を供給する際、均圧管を通つて気液分離器か
ら受液器へ流入するガス冷媒をアキユムレータの
低温部で凝縮させ受液器へヒートポンプサイクル
高圧液冷媒が流入する際、受液器のガス部容積減
少に伴なう受液器圧力上昇を防止し受液器への液
冷媒流入が円滑となり、その結果気液分離器への
受液器からの液冷媒供給が不足することなく冷媒
加熱器での冷媒熱分解が防止できシステムの信頼
性が向上すると共に機器のコンパクト化が可能と
なり、外気温度の影響の少ない快適な暖房装置が
得られるものである。
Effects of the Invention As described above, according to the heating device of the present invention, the accumulator of the heat pump cycle and the liquid receiver are integrated, so when supplying liquid refrigerant from the liquid receiver to the gas-liquid separator, the pressure equalizing pipe is used. The gas refrigerant that flows from the gas-liquid separator to the liquid receiver is condensed in the low temperature section of the accumulator, and when the heat pump cycle high-pressure liquid refrigerant flows into the liquid receiver, the gas refrigerant that flows into the liquid receiver from the gas liquid separator is condensed. Prevents pressure rise in the liquid container and allows smooth flow of liquid refrigerant into the liquid receiver.As a result, there is no shortage of liquid refrigerant supplied from the liquid receiver to the gas-liquid separator, and refrigerant thermal decomposition in the refrigerant heater is prevented. This improves the reliability of the system, makes the equipment more compact, and provides a comfortable heating system that is less affected by outside temperature.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例による暖房装置の回
路構成図、第2図は従来の暖房装置の回路構成図
である。 10……圧縮機、11……凝縮器、12……減
圧装置、13……蒸発器、14……アキユムレー
タ、15……受液器、16……仕切り板、17…
…第1逆止弁、18……気液分離器、19……第
2逆止弁、20……ガス戻し管、21……開閉
弁、22……均圧管、25……冷媒加熱器。
FIG. 1 is a circuit diagram of a heating device according to an embodiment of the present invention, and FIG. 2 is a circuit diagram of a conventional heating device. 10... Compressor, 11... Condenser, 12... Pressure reducing device, 13... Evaporator, 14... Accumulator, 15... Liquid receiver, 16... Partition plate, 17...
... first check valve, 18 ... gas-liquid separator, 19 ... second check valve, 20 ... gas return pipe, 21 ... on-off valve, 22 ... pressure equalization pipe, 25 ... refrigerant heater.

Claims (1)

【特許請求の範囲】[Claims] 1 圧縮機、アキユムレータ、凝縮器、減圧装
置、蒸発器とからなるヒートポンプサイクルを有
し、前記ヒートポンプサイクルの高圧液部から第
1逆止弁を介し連結した受液器、前記受液器の下
方に第2逆止弁を介して連結した気液分離器、前
記気液分離器からガス戻し管を前記圧縮機吐出管
と、開閉弁を有する均圧管を前記受液器と各々連
結すると共に、前記気液分離器の液管と戻り管を
冷媒加熱器と連結したサイクルとからなり、仕切
り板により2つの空間を形成する容器の一方を前
記アキユムレータ、他方を前記受液器としてなる
暖房装置。
1. A heat pump cycle comprising a compressor, an accumulator, a condenser, a pressure reducer, and an evaporator, and a liquid receiver connected from the high-pressure liquid part of the heat pump cycle via a first check valve, below the liquid receiver. a gas-liquid separator connected to the gas-liquid separator via a second check valve, a gas return pipe from the gas-liquid separator connected to the compressor discharge pipe, and a pressure equalization pipe having an on-off valve connected to the liquid receiver, respectively; A heating device comprising a cycle in which a liquid pipe and a return pipe of the gas-liquid separator are connected to a refrigerant heater, and a container forming two spaces with a partition plate, one of which serves as the accumulator and the other as the liquid receiver.
JP28356285A 1985-12-17 1985-12-17 Heating apparatus Granted JPS62142964A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28356285A JPS62142964A (en) 1985-12-17 1985-12-17 Heating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28356285A JPS62142964A (en) 1985-12-17 1985-12-17 Heating apparatus

Publications (2)

Publication Number Publication Date
JPS62142964A JPS62142964A (en) 1987-06-26
JPH0566502B2 true JPH0566502B2 (en) 1993-09-21

Family

ID=17667134

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28356285A Granted JPS62142964A (en) 1985-12-17 1985-12-17 Heating apparatus

Country Status (1)

Country Link
JP (1) JPS62142964A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS553321U (en) * 1978-06-19 1980-01-10
JPS6071862A (en) * 1983-09-28 1985-04-23 松下電器産業株式会社 Heat pump device
JPS6089627A (en) * 1983-10-21 1985-05-20 Mitsubishi Electric Corp Heating device

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS553321U (en) * 1978-06-19 1980-01-10
JPS6071862A (en) * 1983-09-28 1985-04-23 松下電器産業株式会社 Heat pump device
JPS6089627A (en) * 1983-10-21 1985-05-20 Mitsubishi Electric Corp Heating device

Also Published As

Publication number Publication date
JPS62142964A (en) 1987-06-26

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