JPH05321613A - Heat using device and impurity removal device therefor - Google Patents

Heat using device and impurity removal device therefor

Info

Publication number
JPH05321613A
JPH05321613A JP13243192A JP13243192A JPH05321613A JP H05321613 A JPH05321613 A JP H05321613A JP 13243192 A JP13243192 A JP 13243192A JP 13243192 A JP13243192 A JP 13243192A JP H05321613 A JPH05321613 A JP H05321613A
Authority
JP
Japan
Prior art keywords
heat medium
heat
impurity
impurity removal
removal cylinder
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.)
Pending
Application number
JP13243192A
Other languages
Japanese (ja)
Inventor
Yosaburo Iwato
要三良 岩藤
Junji Ogata
潤司 緒方
Yoshio Shimada
良夫 島田
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 Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP13243192A priority Critical patent/JPH05321613A/en
Publication of JPH05321613A publication Critical patent/JPH05321613A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To effectively remove impurities from a heat medium in a heat using device using dielectric liquid as the heat medium. CONSTITUTION:A heat using device comprising a heat medium evaporator 1, a turbine 3 and a condenser 5 has a heat medium circulating system 8 from which an impurity removal device 23 branches. The device 23 has a moisture removal cylinder 11 and an impurity removal cylinder 10, the moisture removal cylinder 11 removing moisture as an impurity from the heat medium branching from the heat medium circulating system 8, and thereafter the heat medium being led between positive and negative electrodes connected to an d.c. source within the impurity removal cylinder 10 so that ions as an impurity in the heat medium, is separated and attracted to the negative electrode having a positive polarity. The separated impurity ions are eluted again when the power fed to the electrodes in the impurity removal cylinder 10 is cut off after a branch valve 13 is closed, and accordingly, are discharged outside of the system by opening a blow valve 15.

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、有機媒体発電システム
やフロン等を熱媒体とするヒートポンプなど誘電液体を
熱媒体とする熱利用装置に関し、特に前記熱媒体から不
純物を電気的に除去する装置を備えた熱利用装置に関す
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heat utilization device using a dielectric liquid as a heat medium, such as an organic medium power generation system and a heat pump using freon as a heat medium, and more particularly to a device for electrically removing impurities from the heat medium. The present invention relates to a heat utilization device.

【0002】[0002]

【従来の技術】誘電液体を熱媒体とする熱利用装置の1
つとして有機媒体発電システムやフロンを使った、ヒー
トポンプ式冷凍装置があるが、この有機媒体発電システ
ムは、廃蒸気等を熱源として蒸発器内で熱媒体を蒸発さ
せて、タービンに導き蒸気の膨脹によってタービンを回
転させ発電機を駆動させそのあと熱媒体蒸気を凝縮器で
凝縮させ再度循環ポンプで蒸発器に送られる所謂ランキ
ンサイクル発電システムである。
2. Description of the Related Art 1 of heat utilization device using dielectric liquid as heat medium
There is a heat pump type refrigeration system that uses an organic medium power generation system and CFCs, but this organic medium power generation system evaporates the heat medium in the evaporator using waste steam as a heat source and guides it to the turbine to expand the steam. This is a so-called Rankine cycle power generation system in which the turbine is rotated to drive the generator, the heat medium vapor is condensed in the condenser, and then sent to the evaporator by the circulation pump again.

【0003】この様なシステムにおいて、利用される有
機媒体としての特定フロン(ハロゲン化炭化弗素)は、
周知のごとく、オゾン層破壊の元凶とされて国際協定に
より今世紀末を以て全廃され製造禁止となる。
In such a system, the specific fluorocarbon (halogenated fluorocarbon) used as an organic medium is
As is well known, it is considered to be the cause of the ozone layer depletion, and due to an international agreement, it will be completely abolished at the end of this century and production will be banned.

【0004】従来、有機媒体発電システム或いは冷凍機
におけるヒートポンプの熱媒体としてフロンR11が最
も広く用いられていたが、R11は特定フロンに該当す
るためその代替冷媒としてR123が製品化されてい
る。
Conventionally, chlorofluorocarbon R11 has been most widely used as a heat medium for a heat pump in an organic medium power generation system or a refrigerator, but since R11 corresponds to a specific chlorofluorocarbon, R123 has been commercialized as an alternative refrigerant.

【0005】一方、本発明者等の実験によって、代替冷
媒R123は、従来のフロンR11に比べ電気抵抗(導
電率)が低いため、これら、熱媒体の為の蒸発器(電気
流体力学的技術利用)における消費電流の増大及び系統
に直接組み込まれているフロン循環ポンプ(キャンドポ
ンプ)等の電気絶縁破壊を生ずる危惧を有する欠点が判
明した。
On the other hand, according to experiments by the present inventors, the alternative refrigerant R123 has a lower electric resistance (conductivity) than the conventional CFC R11. ), There is a risk of increasing the current consumption and causing electric insulation breakdown of the CFC circulation pump (canned pump) directly incorporated in the system.

【0006】[0006]

【発明が解決しようとする課題】誘電液体を熱媒体とす
る熱利用装置における前記したような熱媒体に関する問
題点としての電気絶縁性の低下及び高電圧印加による消
費電流の増加の主要因は冷媒R123に含まれる水分、
弗素イオン等の不純物及び装置の接液部から溶質する不
純物(Fe- ,Cl - ,Na - ) によるものであり熱媒体液中
に含まれる微量の不純物を除去することにより、前記不
具合を解決することが可能である。
The main causes of the deterioration of the electrical insulation and the increase of the consumption current due to the application of high voltage as the problems relating to the heat medium as described above in the heat utilization device using the dielectric liquid as the heat medium are the refrigerants. Moisture contained in R123,
Impurities and impurities solutes from wetted parts of the device such as a fluorine ion (Fe -, Cl -, Na -) by removing trace impurities contained in the and the heat medium liquid due, to solve the problem It is possible.

【0007】従って、本発明は、このように誘電液体を
熱媒体とする熱利用装置における熱媒体中の不純物によ
って生ずる問題点を解消することを課題としている。
Therefore, the present invention has an object to solve the problems caused by impurities in the heat medium in the heat utilization apparatus using the dielectric liquid as the heat medium.

【0008】[0008]

【課題を解決するための手段】本発明は、誘電液体を熱
媒体とする熱利用装置において、同熱媒体に高電圧を印
加する電極を内装した不純物除去装置を組込み液体中の
分離した汚染媒体を系外へ放出することにより前記した
課題を解決するものである。
DISCLOSURE OF THE INVENTION The present invention relates to a heat utilization device using a dielectric liquid as a heat medium, which incorporates an impurity removing device equipped with electrodes for applying a high voltage to the heat medium, and which is a contaminated medium separated in the liquid. It is intended to solve the above-mentioned problems by releasing the compound out of the system.

【0009】本発明における不純物除去装置は、熱媒体
の流れの中に正極、負極の導電体の電極板を互いに一定
の間隙を保って必要数の電極ブロックを構成させ、一方
の電極に高電圧を印加することによって、電極間に電場
を形成させ流体中の不純物イオンを正極板に吸着させて
分離し、熱媒体中の不純物を分離除去するものである。
In the impurity removing apparatus according to the present invention, a required number of electrode blocks are formed by keeping a constant gap between the electrode plates of the positive and negative conductors in the flow of the heat medium, and one electrode is provided with a high voltage. Is applied to form an electric field between the electrodes so that the impurity ions in the fluid are adsorbed on the positive electrode plate and separated, and the impurities in the heat medium are separated and removed.

【0010】[0010]

【作用】図3に示すごとく、誘電液体(熱媒体)に直流
高電圧を印加すると誘電液体が自己解離作用を起こし不
純物イオン22が電気力によって正電極19側に吸着さ
れ分離される。
As shown in FIG. 3, when a high DC voltage is applied to the dielectric liquid (heat medium), the dielectric liquid causes a self-dissociation action, and the impurity ions 22 are adsorbed and separated on the positive electrode 19 side by an electric force.

【0011】本発明ではこの原理を応用し、熱媒体を系
統内へ充填する際及び系統内の器壁接液部から生じた溶
質物(不純物)の汚染熱媒体を不純物除去装置を通すこ
とにより浄化するものである。
In the present invention, by applying this principle, the contaminated heat medium of the solute (impurity) generated from the liquid contact part on the vessel wall in the system is passed through the impurity removing device when the heat medium is filled into the system. It purifies.

【0012】なお、不純物22の解離が終わると純粋な
熱媒体のもつ電気的特性に見合う誘電体電流値が示さ
れ、不純物22が正電極19側へ分離吸着された事が判
る。
When the impurities 22 are dissociated, a dielectric current value corresponding to the electrical characteristics of the pure heat medium is shown, which shows that the impurities 22 are separated and adsorbed to the positive electrode 19 side.

【0013】従って正常な電流値に達した時点で不純物
除去装置を熱利用装置の熱媒体循環系から切り離し、電
極への直流電源を切ると解離していた不純物は再び液体
中に溶け込む。
Therefore, when the normal current value is reached, the impurity removing device is disconnected from the heat medium circulating system of the heat utilizing device, and when the DC power supply to the electrodes is turned off, the dissociated impurities are dissolved again in the liquid.

【0014】この不純物汚染媒体を系外に放出して熱媒
体中の不純物を除去することができる。以下、本発明を
図示した実施例に基づいて具体的に説明する。
This impurity contaminated medium can be discharged to the outside of the system to remove impurities in the heat medium. Hereinafter, the present invention will be specifically described based on illustrated embodiments.

【0015】[0015]

【実施例】図1は、本発明による、不純物除去装置を組
み込んだ熱利用装置としての有機媒体発電システムを示
し、1は蒸発器で、ここでは廃蒸気等を熱源として熱媒
体を加熱して蒸発させる。蒸発器1で発生した蒸気はタ
ービン3に導かれて蒸気は膨脹してタービン3を回転さ
せて発電機4を駆動する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 shows an organic medium power generation system as a heat utilizing device incorporating an impurity removing device according to the present invention, wherein 1 is an evaporator, in which waste steam or the like is used as a heat source to heat the heating medium. Evaporate. The steam generated in the evaporator 1 is guided to the turbine 3, and the steam expands to rotate the turbine 3 to drive the generator 4.

【0016】そのあと熱媒体の蒸気は凝縮器5で冷却水
供給系6によって冷却されて凝縮され循環ポンプ7によ
って分岐弁9が介在された熱媒体循環系8によって再度
蒸発器1へ送られ、いわゆるランキンサイクル発電シス
テムを形成する。
After that, the vapor of the heat medium is cooled in the condenser 5 by the cooling water supply system 6 and condensed, and is sent to the evaporator 1 again by the heat medium circulation system 8 with the branch valve 9 interposed by the circulation pump 7. Form a so-called Rankine cycle power generation system.

【0017】このようなシステムにおいて利用される熱
媒体としてのR123は、その中に含まれて来る不純物
のため前述のとおり電気絶縁性の低下及び消費電流の増
加が問題となるが、図1に示す有機媒体発電システムで
は、その熱媒体から不純物を除去するための不純物除去
装置23が組み込まれている。
As described above, R123 as a heat medium used in such a system has a problem that the electric insulation is lowered and the current consumption is increased due to impurities contained therein. In the organic medium power generation system shown, an impurity removing device 23 for removing impurities from the heat medium is incorporated.

【0018】不純物除去装置23は、有機媒体発電シス
テムの熱媒体循環系8から熱媒体を分岐する分岐管路1
2、熱媒体中から不純物としての水分を除去する水分除
去筒11、不純物としてのイオンを除去する不純物除去
筒10、及び不純物除去筒へ直流電流を供給する電源1
4を有している。図中、13は分岐弁、15は不純物除
去筒から、不純物を含む熱媒体を排出させるブロー弁で
ある。
The impurity removing device 23 is a branch pipe 1 for branching the heat medium from the heat medium circulation system 8 of the organic medium power generation system.
2, a moisture removing cylinder 11 for removing moisture as an impurity from the heat medium, an impurity removing cylinder 10 for removing ions as impurities, and a power supply 1 for supplying a direct current to the impurity removing cylinder.
Have four. In the figure, 13 is a branch valve, and 15 is a blow valve for discharging the heat medium containing impurities from the impurity removal cylinder.

【0019】図2に示すごとく不純物除去筒10は鋼製
外殻の中に棒状又は板状の正極19、負極18それぞれ
の電極を必要数組合せて内装し、正極側両端はテフロ
ン、又は碍子17等の電気絶縁物によって負極側と絶縁
され一方、負極側は本体外殻に接続し接地されている。
As shown in FIG. 2, the impurity removing cylinder 10 has a steel outer shell in which a rod-shaped or plate-shaped positive electrode 19 and a negative electrode 18 are combined in a required number of electrodes, and both ends of the positive electrode side are made of Teflon or an insulator 17. While being insulated from the negative electrode side by an electric insulator such as, the negative electrode side is connected to the outer shell of the main body and grounded.

【0020】不純物除去筒10は円筒形であってよく、
その中に正極性電極と負極性板を半径方向に交互に配設
したものとして構成できる。この水分除去筒は2本を並
列に設け、交互に使用しても良い。
The impurity removal cylinder 10 may be cylindrical,
A positive electrode and a negative plate may be alternately arranged in the radial direction. Two water removing cylinders may be provided in parallel and used alternately.

【0021】なお図1の分岐管路12の上流側に接続し
ている水分除去筒11は在来技術(円筒に水分吸収剤充
填)の応用であり詳細な説明は省略する。
The water removing cylinder 11 connected to the upstream side of the branch conduit 12 in FIG. 1 is an application of a conventional technique (filling a water absorbent with a cylinder), and a detailed description thereof will be omitted.

【0022】このように構成された有機媒体発電システ
ムにおいて、システム中の熱媒体に不純物が入って来て
電流値が正常な値に達しなくなったら、分岐弁13を開
いて熱媒体循環系8から不純物除去装置23へ熱媒体を
分岐する。
In the organic medium power generation system thus constructed, when impurities enter the heat medium in the system and the current value does not reach the normal value, the branch valve 13 is opened to remove heat from the heat medium circulation system 8. The heat medium is branched to the impurity removing device 23.

【0023】この状態で不純物除去筒10に直流高電圧
を印加する。不純物イオンが電気力によって正電極側に
吸着され熱媒体中から分離される。熱媒体中の不純物を
正電極側へ吸着分離したら、分岐弁13を閉じて不純物
除去装置23を熱媒体循環系8から切り離し、不純物除
去筒10の電源を切る。
In this state, a DC high voltage is applied to the impurity removing cylinder 10. Impurity ions are adsorbed to the positive electrode side by electric force and separated from the heat medium. After the impurities in the heat medium are adsorbed and separated to the positive electrode side, the branch valve 13 is closed to disconnect the impurity removing device 23 from the heat medium circulating system 8, and the impurity removing cylinder 10 is powered off.

【0024】不純物除去操作におって正電極側へ分離さ
れていた不純物は再び液体中に溶け出すのでブロー弁1
5を開いて系外に排出する。
Since the impurities separated on the positive electrode side during the impurity removal operation are dissolved again in the liquid, the blow valve 1
Open 5 and discharge to the outside of the system.

【0025】以上、本発明による装置の1実施例につい
て説明したが、不純物除去装置23の具体的構成や不純
物除去筒の構造などについては種々の変更を加えてもよ
いことは勿論である。例えば、不純物除去筒10の電極
配置としては、正極,負極を同心円状に多重に配置して
もよい。
Although one embodiment of the apparatus according to the present invention has been described above, it goes without saying that various modifications may be made to the specific structure of the impurity removing apparatus 23 and the structure of the impurity removing cylinder. For example, as the electrode arrangement of the impurity removal cylinder 10, the positive electrode and the negative electrode may be concentrically arranged in multiple layers.

【0026】[0026]

【発明の効果】既に記述したごとく、特定フロン規判に
伴う代替冷媒R123は微量に含まれる不純物(F - ,
Fe- ,Na - , Cl- 等)及び水分によって電気的物性の変
化に影響を来し、これらの媒体を使った熱利用システム
機器の性能低下とトラブルの起因となっていたが、本発
明による電気的不純物除去装置23によってプラント稼
働状態のまヽで熱媒体の精製が可能となり、プラント全
体の信頼性向上と運転コストの低減,性能向上に寄与で
きる。
Effects of the Invention As already described, the impurity (F replacement refrigerants R123 accompanying CFCs Tadashiban contained in trace amounts -,
Fe -, Na -, Cl -, etc.) and Kitashi an effect on changes in electrical properties due to moisture, it had become due for performance degradation and trouble heat utilization system equipment using these media, according to the invention The electric impurity removing device 23 enables the heat medium to be refined while the plant is operating, and contributes to the improvement of the reliability of the entire plant, the reduction of operating cost, and the improvement of performance.

【0027】一例として、EHD(電気流体力学)技術
利用の高性能蒸発器においては、熱媒体中の不純物を除
去することによって、EHD消費電流が半減されるた
め、プラント全体のシステム熱効率が上昇し、高性能蒸
発器本来の小形コンパクト化による大巾なコスト低減が
達成される。
As an example, in a high-performance evaporator using EHD (electrohydrodynamics) technology, the impurities in the heat medium are removed to reduce the EHD consumption current by half, thereby increasing the system thermal efficiency of the entire plant. A large cost reduction can be achieved by making the high performance evaporator originally small and compact.

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

【図1】本発明の第1実施例に係る熱利用プラント全体
の系統図。
FIG. 1 is a system diagram of an entire heat utilization plant according to a first embodiment of the present invention.

【図2】本発明による装置で用いる不純物除去筒の1実
施例における構成図。
FIG. 2 is a structural view of an impurity removal cylinder used in the apparatus according to the present invention in one embodiment.

【図3】本発明に係る装置における不純物除去作用の説
明図。
FIG. 3 is an explanatory diagram of an impurity removing action in the device according to the present invention.

【符号の説明】[Explanation of symbols]

1 蒸発器 2 熱源供給系 3 タービン 4 発電機 5 凝縮器 6 冷却水供給系 7 循環ポンプ 8 熱媒体循環系 9 分岐弁 10 不純物除去筒 11 水分除去筒 12 分岐管路 13 分岐弁 14 直流電源装置 15 ブロー弁 16 電極リード 17 絶縁碍子 18 負極性板 19 正極性電極 20 EHD伝熱蒸発管 21 EHD電源 22 不純物イオン 23 不純物除去装置 1 Evaporator 2 Heat Source Supply System 3 Turbine 4 Generator 5 Condenser 6 Cooling Water Supply System 7 Circulation Pump 8 Heat Medium Circulation System 9 Branch Valve 10 Impurity Removal Cylinder 11 Moisture Removal Cylinder 12 Branch Pipeline 13 Branch Valve 14 DC Power Supply 15 Blow Valve 16 Electrode Lead 17 Insulator 18 Negative Plate 19 Positive Electrode 20 EHD Heat Transfer Evaporator 21 EHD Power Supply 22 Impurity Ion 23 Impurity Removal Device

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 誘電液体を熱媒体とする熱利用装置にお
いて、前記熱媒体に高電圧を印加して前記熱媒体中の不
純物イオンを電気的に分離除去する不純物除去装置を前
記熱媒体循環系統に備えたことを特徴とする熱利用装
置。
1. A heat utilizing apparatus using a dielectric liquid as a heat medium, wherein the heat medium circulating system is an impurity removing apparatus for applying a high voltage to the heat medium to electrically separate and remove impurity ions in the heat medium. A heat utilization device characterized in that
【請求項2】 正極と負極が半径方向に交互に配設され
た不純物除去筒、および前記正極と負極に高電圧を印加
する直流電源装置を有することを特徴とする誘電液体を
熱媒体として使う熱利用装置のための不純物除去装置。
2. A dielectric liquid is used as a heat medium, which comprises an impurity removing cylinder in which positive electrodes and negative electrodes are alternately arranged in a radial direction, and a DC power supply device for applying a high voltage to the positive electrodes and negative electrodes. Impurity remover for heat utilization equipment.
JP13243192A 1992-05-25 1992-05-25 Heat using device and impurity removal device therefor Pending JPH05321613A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13243192A JPH05321613A (en) 1992-05-25 1992-05-25 Heat using device and impurity removal device therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13243192A JPH05321613A (en) 1992-05-25 1992-05-25 Heat using device and impurity removal device therefor

Publications (1)

Publication Number Publication Date
JPH05321613A true JPH05321613A (en) 1993-12-07

Family

ID=15081220

Family Applications (1)

Application Number Title Priority Date Filing Date
JP13243192A Pending JPH05321613A (en) 1992-05-25 1992-05-25 Heat using device and impurity removal device therefor

Country Status (1)

Country Link
JP (1) JPH05321613A (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62195734A (en) * 1986-08-29 1987-08-28 Hitachi Ltd Detecting system for out of focus or out of track of objective optical system
WO1996012921A1 (en) * 1994-10-25 1996-05-02 Daikin Industries, Ltd. Air conditioner and method of controlling washing operation thereof
JP2014194216A (en) * 2013-02-26 2014-10-09 Kobe Steel Ltd Binary power generator operation method
KR20180028164A (en) * 2016-09-08 2018-03-16 현대중공업 주식회사 A Regasification System Of Gas and Vessel having same
KR20180138526A (en) * 2017-06-21 2018-12-31 가부시키가이샤 고베 세이코쇼 Impurity recovery method and oil recovery method
KR102152461B1 (en) * 2019-04-11 2020-09-07 한국기계연구원 Generating system for organic rankine cycle and control method for the same
CN112186291A (en) * 2019-07-03 2021-01-05 本田技研工业株式会社 Heat cycle system
JP2021008871A (en) * 2019-07-03 2021-01-28 本田技研工業株式会社 Heat cycle system
JP2021008872A (en) * 2019-07-03 2021-01-28 本田技研工業株式会社 Heat cycle system

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62195734A (en) * 1986-08-29 1987-08-28 Hitachi Ltd Detecting system for out of focus or out of track of objective optical system
WO1996012921A1 (en) * 1994-10-25 1996-05-02 Daikin Industries, Ltd. Air conditioner and method of controlling washing operation thereof
JP2014194216A (en) * 2013-02-26 2014-10-09 Kobe Steel Ltd Binary power generator operation method
KR20180028164A (en) * 2016-09-08 2018-03-16 현대중공업 주식회사 A Regasification System Of Gas and Vessel having same
KR20180138526A (en) * 2017-06-21 2018-12-31 가부시키가이샤 고베 세이코쇼 Impurity recovery method and oil recovery method
KR102152461B1 (en) * 2019-04-11 2020-09-07 한국기계연구원 Generating system for organic rankine cycle and control method for the same
CN112186291A (en) * 2019-07-03 2021-01-05 本田技研工业株式会社 Heat cycle system
JP2021008870A (en) * 2019-07-03 2021-01-28 本田技研工業株式会社 Heat cycle system
JP2021008871A (en) * 2019-07-03 2021-01-28 本田技研工業株式会社 Heat cycle system
JP2021008872A (en) * 2019-07-03 2021-01-28 本田技研工業株式会社 Heat cycle system
CN112186291B (en) * 2019-07-03 2024-04-19 本田技研工业株式会社 Thermal circulation system

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