JPH0354846B2 - - Google Patents
Info
- Publication number
- JPH0354846B2 JPH0354846B2 JP15746885A JP15746885A JPH0354846B2 JP H0354846 B2 JPH0354846 B2 JP H0354846B2 JP 15746885 A JP15746885 A JP 15746885A JP 15746885 A JP15746885 A JP 15746885A JP H0354846 B2 JPH0354846 B2 JP H0354846B2
- Authority
- JP
- Japan
- Prior art keywords
- winding
- condensate
- container
- insulating container
- 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.)
- Expired
Links
- 238000004804 winding Methods 0.000 claims description 62
- 238000001816 cooling Methods 0.000 claims description 23
- 230000006698 induction Effects 0.000 claims description 23
- 238000004891 communication Methods 0.000 claims description 18
- 239000007788 liquid Substances 0.000 claims description 16
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical group [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 7
- 230000001105 regulatory effect Effects 0.000 claims description 4
- 238000001514 detection method Methods 0.000 claims 1
- 239000012212 insulator Substances 0.000 claims 1
- 230000005684 electric field Effects 0.000 description 14
- 239000002826 coolant Substances 0.000 description 9
- 238000009835 boiling Methods 0.000 description 8
- 238000009413 insulation Methods 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 230000006866 deterioration Effects 0.000 description 4
- 239000006185 dispersion Substances 0.000 description 3
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 3
- 239000007791 liquid phase Substances 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Transformer Cooling (AREA)
Description
【発明の詳細な説明】
〔発明の属する技術分野〕
本発明は非凝縮性の絶縁ガスと凝縮性の冷却媒
体とを密閉絶縁容器によつて分離したセパレート
形の蒸発冷却誘導電器に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of the Invention] The present invention relates to a separate type evaporative cooling induction electric appliance in which a non-condensable insulating gas and a condensable cooling medium are separated by a closed insulating container.
近年、主として防災上の見地から高電圧大容量
の変圧器、リアクトル等の誘導電器の不燃化、難
燃化の要求が高まり、従来の油入電器に代つて不
燃性、絶縁性、凝縮性を有するフロロカーボン、
フロン等の凝縮液を冷却媒体とし、SF6ガス等の
絶縁ガスを絶縁媒体とした蒸発冷却誘導電器が注
目されており、絶縁油に比べて格段に高価な冷却
媒体の使用量が少く冷却性能が優れるとともに、
高電圧化が可能な誘導電器が求められている。
In recent years, there has been an increasing demand for high-voltage, large-capacity transformers, reactors, and other induction electrical appliances to be non-combustible and flame-retardant, mainly from the standpoint of disaster prevention. fluorocarbon, having
Evaporative cooling induction electric appliances that use condensate such as Freon as a cooling medium and insulating gas such as SF 6 gas as an insulating medium are attracting attention, and compared to insulating oil, they use much less expensive cooling medium and have better cooling performance. In addition to being excellent,
There is a need for induction electric appliances that can handle high voltage.
第5図は散布形、第6図はセパレート形の蒸発
冷却誘導電器のそれぞれ一例を示す概略側断面図
である。凝縮液散布形の場合、冷却媒体10およ
び絶縁ガス9を包蔵したタンク1に収納され鉄心
2に巻装された複数のセクシヨンコイル4および
セクシヨン間ダクト7からなる円板巻線3は巻線
を包囲するよう形成された絶縁容器5に収納され
るとともに、凝縮液の移送手段11ないし13を
介して鉄心2の上方に配された散布装置14に移
送され小孔15を介して散布される凝縮液10の
液流10Aを受けて鉄心2が蒸発冷却されるとと
もに、絶縁容器5に貯留された凝縮液10中に浸
漬された円板巻線が凝縮液の蒸発潜熱により冷却
され、気化した凝縮液の蒸気10Bは凝縮器6で
再び凝縮されてタンク1の底部に復帰するよう構
成されている。 FIG. 5 is a schematic side sectional view showing an example of an evaporative cooling induction electric appliance, and FIG. 6 is a schematic side sectional view showing an example of an evaporative cooling induction electric appliance of a dispersion type and FIG. 6 of a separate type. In the case of the condensate dispersion type, the disk winding 3 is housed in a tank 1 containing a cooling medium 10 and an insulating gas 9, and is made up of a plurality of section coils 4 and an inter-section duct 7 wound around an iron core 2. The condensate is stored in an insulating container 5 formed to surround it, and is transferred via condensate transfer means 11 to 13 to a dispersion device 14 disposed above the iron core 2, where it is dispersed through small holes 15. The iron core 2 is evaporatively cooled by receiving the liquid flow 10A of the condensate 10, and the disc winding immersed in the condensate 10 stored in the insulating container 5 is cooled by the latent heat of evaporation of the condensate and vaporized. The condensed liquid vapor 10B is condensed again in the condenser 6 and returned to the bottom of the tank 1.
上述のように構成された散布形の蒸発冷却誘導
電器においては鉄心と巻線を同時にかつ液枯れを
生ずることなく効率よく蒸発冷却できる反面、凝
縮液10の貯留部が3個所にわたるために高価な
凝縮液の使用量が多く経済的不利益をもたらすと
ともに、巻線の冷却を凝縮液の蒸発潜熱のみに依
存しているために、巻線温度が冷欺媒体の沸点温
度に大幅に左右されるという問題があり、誘導電
器の電気的負荷の増大に伴なつて絶縁槽5中に多
量の気泡が発生し、巻線3の耐電圧性能が低下す
るという問題がある。 In the scatter type evaporative cooling induction electric appliance constructed as described above, the iron core and the winding can be simultaneously and efficiently evaporatively cooled without causing liquid drying up. The large amount of condensate used creates an economic disadvantage, and since winding cooling relies solely on the latent heat of vaporization of the condensate, the winding temperature is significantly dependent on the boiling point temperature of the cooling medium. There is a problem in that as the electrical load of the induction appliance increases, a large amount of bubbles are generated in the insulation tank 5, and the withstand voltage performance of the winding 3 is reduced.
一方第6図に示すセパレート形においては、円
板巻線3が密閉絶縁容器25に収納され、上下一
対の循環通路22,23を介して循環ポンプ21
および熱交換器26に連結され、密閉絶縁容器2
5、熱交換器26等の閉鎖循環系統内に巻線3が
浸漬されるよう包蔵された凝縮液10とタンク1
内に包蔵された絶縁ガス9とを分離するよう形成
されるとともに、ポンプ21により密閉絶縁容器
25および熱交換器26間を循環する凝縮液10
の顕熱および潜熱の両方を利用して巻線3を冷却
するよう構成されている。したがつて凝縮液の使
用量を低減できるとともに、巻線の冷却に凝縮液
の顕熱と潜熱とを利用できることにより、冷却媒
体の沸点温度の制約が少く、冷却性能と価格とを
総合的に評価して有利な冷却媒体を選択できる利
点がある。 On the other hand, in the separate type shown in FIG.
and a heat exchanger 26, the sealed insulating container 2
5. A condensate 10 and a tank 1 contained in a closed circulation system such as a heat exchanger 26 so that the winding 3 is immersed therein.
A condensate 10 is formed to separate the insulating gas 9 contained therein, and is circulated between the closed insulating container 25 and the heat exchanger 26 by the pump 21.
The winding 3 is configured to be cooled using both sensible heat and latent heat. Therefore, the amount of condensate used can be reduced, and the sensible heat and latent heat of the condensate can be used to cool the windings, so there are fewer restrictions on the boiling point temperature of the cooling medium, and it is possible to achieve a comprehensive combination of cooling performance and price. It has the advantage of being able to evaluate and select an advantageous cooling medium.
ところで一般に、凝縮性の冷却媒体の耐電圧性
能は液相で高く、気相で低い性質を持つているの
で、散布形、セパレート形のいずれにおいても局
部的電界集中部の多い巻線を凝縮液に浸漬して液
相絶縁するとともに、局部的電界集中部の少い巻
線から離れた空間部をガス絶縁することにより、
耐電圧性能にすぐれた誘導電器、いいかえれば高
電圧化が可能な誘導電器が得られる利点を有す
る。ところが、巻線が浸漬された凝縮液を沸騰す
ることにより巻線近傍は気液混合絶縁になるため
に冷却性能の向上に逆行して耐電圧性能が低下す
るという問題があり、これが原因で高電圧化が阻
害されるという欠点がある。 By the way, in general, the withstand voltage performance of condensable cooling media is high in the liquid phase and low in the gas phase, so whether the windings have many localized electric field concentration parts in either the dispersed type or the separate type, By immersing it in liquid phase insulation and insulating the space away from the winding where there is little local electric field concentration,
It has the advantage of providing an induction electric appliance with excellent withstand voltage performance, in other words, an induction electric appliance that can be used at high voltages. However, as the condensate in which the windings are immersed is boiled, the area around the windings becomes a mixed gas-liquid insulation, which goes against the improvement of cooling performance and reduces withstand voltage performance. There is a drawback that voltage conversion is inhibited.
第7図は上述の状態を示す要部の側断面図であ
り、複数のセクシヨンコイル4およびセクシヨン
間ダクト7からなる円板巻線の内、外周側は軸方
向ダクト8を保持するよう絶縁容器5または15
内に収納され、容器内には凝縮液10が、容器の
外側の空間部には絶縁ガス9が充填されているも
のと仮定する。このような状態において巻線容易
に電圧を印加すると、セクシヨンコイル間の電位
差やセクシヨンコイルの対地電位により、セクシ
ヨンコイル4の角部に局部的に電界が集中し、角
部近傍の凝縮液10C部分に高電界部が発生す
る。いま、巻線に流れる電流によつてセクシヨン
コイルの温度が上昇し、凝縮液10の沸点温度を
超えると、セクシヨンコイル4の表面に接触した
凝縮液が沸騰しはじめ、気化した蒸気が気泡とな
つてセクシヨンコイルの下面や側面を伝わつて浮
上するため軸方向ダクト8に気泡が集まり、軸方
向ダクト中を浮上する過程で気泡10Dが生長
し、軸方向上位に位置するセクシヨンコイルの角
部程気泡密度が高い図のような状態が出現する。
このような状態においては、気泡10Dは高電界
にさらされるばかりか、凝縮液に比べて誘電率が
小さいために静電容量分圧の原理に基づいて気泡
にさらに電界が集中するために、液相に比べて耐
電圧強度の低い気泡中で火花放電が発生し、これ
が引き金となつてセクシヨンコイル間が絶縁破壊
するなどの絶縁事故に発展する危険性があり、こ
の種誘導電器の高電圧化を阻害する重大な弱点に
なつている。 FIG. 7 is a side sectional view of the main part showing the above-mentioned state, and the outer circumferential side of the disc winding consisting of a plurality of section coils 4 and the inter-section duct 7 is insulated to hold the axial duct 8. Container 5 or 15
It is assumed that the container is filled with condensate 10 and the space outside the container is filled with insulating gas 9. If a voltage is easily applied to the winding in such a state, the electric field will be locally concentrated at the corner of the section coil 4 due to the potential difference between the section coils and the ground potential of the section coil, causing condensation near the corner. A high electric field portion is generated in the liquid 10C portion. Now, when the temperature of the section coil rises due to the current flowing through the winding and exceeds the boiling point temperature of the condensate 10, the condensate in contact with the surface of the section coil 4 begins to boil, and the vaporized vapor becomes bubbles. The air bubbles gather in the axial duct 8 as the air bubbles float along the lower and side surfaces of the section coil, and during the process of floating through the axial duct, air bubbles 10D grow, causing the air bubbles 10D to float along the axially upper side of the section coil. A state as shown in the figure appears, where the bubble density is higher at the corners.
In such a state, the bubble 10D is not only exposed to a high electric field, but also has a smaller dielectric constant than the condensed liquid, so the electric field concentrates on the bubble based on the principle of capacitance partial pressure, and the liquid There is a risk that spark discharge will occur in the bubbles, which have a lower withstand voltage strength than the phase, and this will trigger an insulation accident such as dielectric breakdown between the section coils. This has become a serious weakness that hinders the development of society.
また第5図に示す散布形のように絶縁層5中の
凝縮液10の液面に絶縁ガス9の圧力を加えるこ
とにより、蒸気気泡10が押しづぶされて耐電圧
強度が上昇することが期待されるが、ゲージ圧
0.5〜1気圧程度のガス圧を加えることにより到
達し得る気相の耐電圧強度は液相のそれの二分の
一程度に止まり、蒸気気泡の影響を排除できない
という問題があり、より一層の改善が求められて
いる。 Furthermore, by applying the pressure of the insulating gas 9 to the liquid level of the condensate 10 in the insulating layer 5 as shown in the scattering type shown in FIG. 5, the steam bubbles 10 can be crushed and the withstand voltage strength can be increased. Expected, but gauge pressure
The withstand voltage strength of the gas phase that can be achieved by applying a gas pressure of about 0.5 to 1 atm is only about half that of the liquid phase, and there is a problem that the influence of vapor bubbles cannot be eliminated, so further improvement is required. is required.
本発明は前述の状況に鑑みてなされたもので、
凝縮液の沸騰に伴なつて生ずる蒸気気泡が巻線の
耐電圧性能に及ぼす影響が排除され、したがつて
耐電圧性能の優れたセパレート形の蒸発冷却誘導
電器を提供することを目的とする。
The present invention was made in view of the above-mentioned situation, and
It is an object of the present invention to provide a separate type evaporative cooling induction electric appliance which eliminates the influence of vapor bubbles generated as a result of boiling of condensate on the withstand voltage performance of the windings, and has excellent withstand voltage performance.
本発明は、巻線を包囲収納し上下一対の循環通
路を介してタンクに外設された熱交換器に連通す
るように形成され前記巻線を浸漬するに足る冷却
媒体の凝縮液を貯えた密閉絶縁容器、ならびにこ
の密閉絶縁容器の内側にこの容器および前記巻線
との間にそれぞれ凝縮液の軸方向通路となるべき
離隔距離を保持するようほぼ同軸状に配設され連
通管を介して前記熱交換器に連通するよう形成さ
れた内側絶縁容器からなる二重の絶縁容器、およ
び内側絶縁容器の側板に両軸方向通路に連通する
よう分布して形成された前記凝縮液の流通孔と、
循環通路および連通管の少なくとも出口側に配設
された流量調整弁とを備え、誘導電器が軽負荷状
態には内側絶縁容器中の巻線内に凝縮液を循環さ
せて顕熱冷却を行い、重負荷時には流量調整弁を
調整することにより内側絶縁容器に流入した凝縮
液を流通孔を介して外側の密閉絶縁容器の軸方向
通路内に導き連通管を介して熱交換器側に循環さ
せるよう構成したことにより、誘導電器の重負荷
時に巻線近傍の凝縮液が沸騰することによつて生
成した蒸気気泡は凝縮液とともに気泡生成部に近
接した流通孔を介して直ちに外側の密閉絶縁容器
の軸方向通路に導かれ巻線近傍から離れるため
に、セクシヨンコイル角部の高電界部に介在する
蒸気気泡を排除できるとともに、軸方向上位に位
置するセクシヨンコイル近傍に気泡が集積するの
を防止でき、したがつて蒸気気泡による耐電圧性
能の低下を阻止できるようにしたものである。
The present invention is configured to surround and house the windings and communicate with a heat exchanger externally installed in a tank through a pair of upper and lower circulation passages, and store enough condensed liquid of a cooling medium to immerse the windings. A hermetically insulated container, and a communication pipe arranged substantially coaxially between the container and the winding to maintain a separation distance between the container and the winding, respectively, to form an axial passage for the condensate. a double insulating container formed of an inner insulating container formed to communicate with the heat exchanger; and a distribution hole for the condensate formed in a side plate of the inner insulating container so as to communicate with both axial passages; ,
It is equipped with a circulation passage and a flow rate regulating valve disposed at least on the outlet side of the communication pipe, and when the induction electric device is under a light load, condensed liquid is circulated within the winding in the inner insulating container to perform sensible heat cooling. During heavy loads, by adjusting the flow rate adjustment valve, the condensate that has flowed into the inner insulated container is guided into the axial passage of the outer sealed insulated container through the communication hole and circulated to the heat exchanger side via the communication pipe. With this structure, steam bubbles generated when the condensate near the windings boils when the induction electric appliance is under heavy load are immediately transferred to the outer airtight insulating container together with the condensate through the flow holes in the vicinity of the bubble generating section. Since the vapor bubbles are guided through the axial passage and away from the vicinity of the winding, it is possible to eliminate the vapor bubbles present in the high electric field area at the corner of the section coil, and also prevent the accumulation of bubbles near the section coil located at the upper position in the axial direction. Therefore, it is possible to prevent deterioration in voltage resistance performance due to vapor bubbles.
以下本発明を実施例に基づいて説明する。 The present invention will be explained below based on examples.
第1図は本発明の実施例を示す概略側断面図で
ある。図において、SF6ガス等の絶縁ガス9を包
蔵したタンク1内に収納された鉄心2に巻装され
た巻線3は、フロロカーボン、フロン等の凝縮性
の冷却媒体の凝縮液10を包蔵しうるよう気密に
形成された密閉絶縁容器35と、この密閉絶縁容
器35の内側に配され密閉絶縁容器35および巻
線3との間にそれぞれ凝縮液10の軸方向通路3
8および39となるべき離隔距離を保持するよう
形成された内側絶縁容器36とからなる二重の絶
縁容器中に収納されている。また密閉絶縁容器3
5は上下一対の循環通路32A,32Bを介して
タンク1に外設された熱交換器26に連結される
とともに上部循環通路32Aには流量調整弁31
Aが設けられ、内側絶縁容器36は側板に分布し
て形成された複数の流通孔37を介して反巻線側
の軸方向通路39に連通するととももに、その上
端部は連通管33および流量調整弁31Bを介し
て熱交換器26に連通し、下端部には給排液弁4
3が設けられている。したがつて凝縮液10は密
閉絶縁容器36、熱交換器26、循環ポンプ21
および循環通路、連通管からなる閉回路内を閉鎖
循環し、タンク1内の絶縁ガス9を包蔵した空間
部と区画され、巻線3の電気的絶縁は巻線近傍は
二重の絶縁容器とその内部に収納された凝縮液1
0によつて、また巻線3から離れた部分は絶縁ガ
ス9によつて保持されている。 FIG. 1 is a schematic side sectional view showing an embodiment of the present invention. In the figure, a winding 3 wound around an iron core 2 housed in a tank 1 containing an insulating gas 9 such as SF 6 gas contains a condensate 10 of a condensable cooling medium such as fluorocarbon or fluorocarbon. An axial passage 3 for the condensate 10 is provided between a hermetically sealed insulating container 35 that is formed to be airtight, and the hermetically insulating container 35 and the winding 3 disposed inside the hermetically sealed insulating container 35.
It is housed in a double insulating container consisting of an inner insulating container 36 formed to maintain a separation distance of 8 and 39. In addition, airtight insulating container 3
5 is connected to a heat exchanger 26 externally installed in the tank 1 via a pair of upper and lower circulation passages 32A, 32B, and a flow rate adjustment valve 31 is connected to the upper circulation passage 32A.
A is provided, and the inner insulating container 36 communicates with the axial passage 39 on the anti-winding side through a plurality of communication holes 37 distributed and formed in the side plate, and the upper end thereof is connected to the communication pipe 33 and It communicates with the heat exchanger 26 via the flow rate adjustment valve 31B, and a liquid supply/drainage valve 4 is provided at the lower end.
3 is provided. Therefore, the condensate 10 is transferred to the closed insulating container 36, the heat exchanger 26, and the circulation pump 21.
The winding 3 is electrically insulated by a double insulating container near the winding. Condensate 1 stored inside it
0 and the part remote from the winding 3 by an insulating gas 9.
上述のように構成された蒸発冷却誘導電器にお
いて、電気的な負荷が軽く巻線温度が凝縮液の沸
点より低い状態においては、流量調整弁31Bを
閉じ、循環通路側の弁31Aを開くことにより、
凝縮液10は内側絶縁容器36内の巻線に接した
軸方向通路38を通つて循環し、巻線を顕熱冷却
することができるとともに、巻線近傍の絶縁は蒸
気気泡を含まない耐電圧強度の高い凝縮液10に
よつて保持され高い耐電圧性能を得ることができ
る。 In the evaporative cooling induction electric appliance configured as described above, when the electrical load is light and the winding temperature is lower than the boiling point of the condensate, the flow adjustment valve 31B is closed and the circulation passage side valve 31A is opened. ,
The condensate 10 is circulated through an axial passage 38 adjacent to the windings in an inner insulating vessel 36 to provide sensible cooling of the windings, while the insulation near the windings has a voltage withstand voltage free from vapor bubbles. It is retained by the highly strong condensate 10, and high withstand voltage performance can be obtained.
つぎに誘導電器の電気的負荷が増大し、巻線温
度が凝縮液の沸点温度を超える状態では循環通路
32A側の流量調整弁31Aをほとんど閉状態と
し、連通管33側の流量調整弁31Bをほとんど
全開状態とすることにより、下部循環通路32B
から内側絶縁容器36の軸方向通路38に流入し
た凝縮液10に流通孔37を介して軸方向通路3
9側に導く径方向の分力を与えることができるの
で、巻線3の各セクシヨンコイルで生成された蒸
気気泡を径方向の分力を利用して凝縮液とともに
反巻線側の軸方向通路39側に排出させることが
できる。したがつて、内側絶縁容器36の側板に
蒸気気泡が通り得る大きさの流通孔37を軸方向
および径方向に分布して形成しておくことによ
り、セクシヨンコイル角部に接した巻線側の軸方
向通路38内の蒸気気泡を速かに排除することが
できるので、蒸気気泡による耐電圧性能の低下を
阻止することができる。 Next, when the electrical load on the induction device increases and the winding temperature exceeds the boiling point temperature of the condensate, the flow rate adjustment valve 31A on the circulation passage 32A side is almost closed, and the flow rate adjustment valve 31B on the communication pipe 33 side is closed. By almost fully opening the lower circulation passage 32B
The condensate 10 flowing into the axial passage 38 of the inner insulating container 36 from the axial passage 3 through the communication hole 37
Since it is possible to apply a radial component force that leads to the winding 3 side, the steam bubbles generated in each section coil of the winding 3 can be pushed along with the condensate in the axial direction on the opposite winding side. It can be discharged to the passage 39 side. Therefore, by forming distribution holes 37 in the side plate of the inner insulating container 36 in a size that allows steam bubbles to pass through, distributed in the axial and radial directions, the winding side in contact with the corner of the section coil is formed. Since the steam bubbles in the axial passage 38 can be quickly removed, it is possible to prevent the voltage withstanding performance from deteriorating due to the steam bubbles.
第2図は前述の実施例における蒸気気泡の状態
を示す説明図であり、セクシヨンコイル4の下方
から軸方向通路38に流入した凝縮液10は流通
孔37を介して反巻線側の軸方向通路39を流入
するので、これら多数の分流によつて生じた径方
向の流れの分力により蒸気気泡10Dは流通孔か
ら軸方向通路39側に流れ出し、蒸気気泡を含ん
だ凝縮液の液流20は軸方向通路39を通つて熱
交換器に導かれる。軸方向通路39は高電界部1
0Cから離れているために気放中で火花放電が発
生する危険性はなく、高電界部10Cの気泡の量
および大きさが大幅に低減されることにより、巻
線の耐電圧性能を大幅に向上することができる。
また各セクシヨンコイルで生成された気泡は側方
に分布して形成された流通孔から排出されて軸方
向通路38の軸方向上位のセクシヨンコイルの角
部に集積滞留するのを阻止できるとともに、軸方
向通路38内の凝縮液の流速は下流側で遅くなる
のに対して軸方向通路39側では逆に速くなるの
で、下流側では蒸気気泡を軸方向通路39側に引
き出す吸い出し作用を自動的に発生させることが
できるので、蒸気気泡をより効果的に排除するこ
とができる。 FIG. 2 is an explanatory diagram showing the state of steam bubbles in the above-described embodiment. Since the steam bubbles 10D flow into the directional passage 39, the component force of the radial flow generated by these many branched flows causes the steam bubbles 10D to flow out from the communication hole toward the axial passage 39, resulting in a liquid flow of condensate containing steam bubbles. 20 is led through an axial passage 39 to a heat exchanger. The axial passage 39 is the high electric field section 1
Since it is far from 0C, there is no risk of spark discharge occurring in the air, and the amount and size of bubbles in the high electric field section 10C is significantly reduced, greatly improving the withstand voltage performance of the winding. can be improved.
In addition, the air bubbles generated in each section coil can be discharged from the distribution holes formed laterally and can be prevented from accumulating and staying at the corner of the axially upper section coil of the axial passage 38. , the flow rate of the condensate in the axial passage 38 is slow on the downstream side, but on the contrary, it becomes faster on the axial passage 39 side. Therefore, on the downstream side, the suction action to draw out the steam bubbles to the axial passage 39 side is automatically performed. steam bubbles can be more effectively eliminated.
なお、第1図において循環通路あるいは連通管
に絶縁ガス空間側に突出したベローズ等の可変容
積部を設け、凝縮液10に絶縁ガス9の圧力が加
わるよう構成すれば、蒸気気泡の内圧を高めるこ
とができ、耐電圧性能をより一層高めることがで
きる。また、流量調整弁31A,31Bを誘導電
器の負荷状態を検知する検知器たとえば変流器か
らの出力信号に基づいて制御するよう構成するこ
とにより、切換作業を省力化できるとともに、顕
熱冷却および沸騰冷却を効率よく行うことができ
る。 In addition, if a variable volume part such as a bellows protruding toward the insulating gas space is provided in the circulation passage or the communication pipe in FIG. 1, and the pressure of the insulating gas 9 is applied to the condensate 10, the internal pressure of the steam bubbles can be increased. This makes it possible to further improve withstand voltage performance. In addition, by configuring the flow rate adjustment valves 31A and 31B to be controlled based on an output signal from a detector, such as a current transformer, that detects the load state of the induction electric device, it is possible to save labor in switching work, and also to realize sensible heat cooling and Boiling cooling can be performed efficiently.
第3図は本発明の異なる実施例を示す要部の側
断面図であり、内側絶縁容器46と巻線3との間
の軸方向通路38を複数のセクシヨンコイル4毎
に閉鎖する液止め49を巻線3の軸方向に内径側
および外径側交互に設けて巻線3のセクシヨン間
ダクト7内に凝縮液10をジグ・ザグ状に流すと
ともに、セクシヨン間ダクト7の流れの下流に対
向する側の内側絶縁容器36の側板部分に流通孔
47を分布して形成するよう構成した点が前述の
実施例と異なつている。 FIG. 3 is a side sectional view of a main part showing a different embodiment of the present invention. 49 are provided alternately on the inner diameter side and the outer diameter side in the axial direction of the winding 3 to cause the condensate 10 to flow in a zig-zag pattern in the inter-section duct 7 of the winding 3, and downstream of the flow in the inter-section duct 7. This embodiment differs from the previous embodiment in that the communication holes 47 are formed in a distributed manner in the side plate portion of the inner insulating container 36 on the opposite side.
第4図は上述の実施例における蒸気気泡の状態
を示す説明図であり、凝縮液をセクシヨン間ダク
ト7にジグ・ザグ状に流すことにより、凝縮液の
流れに径方向の分力を強制的に発生させ、この流
れの分力を直接受ける下流側の側板に分布して形
成された流通孔47を介して蒸気気泡10Dを速
やかに軸方向通路39側に排出することができる
ので、セクシヨンコイル4の下面に付着した蒸気
気泡はもとより、高電界部10C近傍の蒸気気泡
も生長したり集合したりする間もなく排除され、
蒸気気泡による耐電圧性能の低下をより一層効果
的に阻止することができる。 FIG. 4 is an explanatory diagram showing the state of steam bubbles in the above-mentioned embodiment. By flowing the condensate in a zig-zag pattern through the inter-section duct 7, a radial component force is forced on the flow of the condensate. The steam bubbles 10D can be quickly discharged to the axial passage 39 side through the distribution holes 47 formed in the downstream side plate that directly receives the component force of this flow. Not only the steam bubbles attached to the lower surface of the coil 4 but also the steam bubbles near the high electric field section 10C are eliminated before they grow or gather.
Deterioration in voltage resistance performance due to vapor bubbles can be more effectively prevented.
本発明は前述のように、巻線および凝縮液を絶
縁ガス空間と分離して収納し上下一対の循環通路
および流量調整弁を介して熱交換器に連通するよ
う形成された密閉絶縁容器と、この容器の内側に
この容器および巻線それぞれとの間に凝縮液の軸
方向通路となるべき離間距離を保持するよう配さ
れ、側板部に両軸方向通路に連通する流通孔が分
布形成されるとともに、上端部が連通管および流
量調整弁を介して熱交換器に連通するよう形成さ
れた内側絶縁容器とからなる二重の絶縁容器を設
け、誘導電器が軽負荷時には循環通路側の流量調
整弁を主に開いて凝縮液が内側絶縁容器内を軸方
向に環流して顕熱冷却が行われ、重負荷時には連
通管側の流量調整弁を主に開いて凝縮液が流通孔
を介して内側絶縁容器側から外側絶縁容器側に分
布して流れるよう構成した。その結果、顕熱冷却
時には耐電圧強度の高い凝縮液によつて巻線近傍
の高電界部が絶縁されるとともに、重負荷時には
流通孔を介して凝縮液が径方向に移動することに
より凝縮液の流れに径方向の分力が発生し、巻線
の各セクシヨンコイル表面で凝縮液が沸騰するこ
とによつて生じた蒸気気泡を流通孔を介して局部
的電界集中の少い密閉絶縁容器側の軸方向通路側
に排出できるので、セクシヨンコイル角部近傍の
高電界部に蒸気気泡が多く存在することによつて
生ずる巻線の耐電圧性能の低下を阻止することが
でき、絶縁信頼性が高く高電圧化が可能な蒸発冷
却誘導電器を提供することができる。
As described above, the present invention includes a closed insulating container formed to store windings and condensate separately from an insulating gas space and communicate with a heat exchanger via a pair of upper and lower circulation passages and a flow rate regulating valve; Inside the container, the container and each of the windings are arranged to maintain a distance that should form an axial passage for the condensate, and distribution holes communicating with both axial passages are formed in the side plate. In addition, a double insulating container is provided with an inner insulating container whose upper end is formed to communicate with the heat exchanger via a communication pipe and a flow rate adjustment valve, and when the induction device is under light load, the flow rate on the circulation passage side is adjusted. When the valve is mainly opened, the condensate circulates in the axial direction inside the inner insulated container to perform sensible heat cooling.When the load is heavy, the flow rate adjustment valve on the communication pipe side is mainly opened and the condensate flows through the circulation hole. It was configured so that the flow was distributed from the inner insulating container side to the outer insulating container side. As a result, during sensible heat cooling, the high electric field area near the windings is insulated by the condensate with high withstand voltage strength, and when the load is heavy, the condensate moves radially through the flow holes, causing the condensate to cool. A radial component force is generated in the flow of the winding, and the steam bubbles generated by the boiling of the condensate on the surface of each section of the winding are passed through the flow holes into a closed insulating container with little local electric field concentration. Since it can be discharged to the axial passage side of the side, it is possible to prevent the deterioration of the withstand voltage performance of the winding caused by the presence of many steam bubbles in the high electric field area near the corner of the section coil, improving insulation reliability. Therefore, it is possible to provide an evaporative cooling induction electric appliance with high performance and high voltage.
また流通孔によつて互いに連通した巻線側、反
巻線側の軸方向通路内の凝縮液の流速は下流側に
ゆくにしたがつて巻線側で低く、反巻線側で高く
なるので流通孔を介して蒸気気泡を反巻線側の軸
方向通路側に吸い出す作用を自然に発生させるこ
とができ、したがつて軸方向の上位に位置するセ
クシヨンコイル近傍ほど蒸気気泡がたまり易く耐
電圧性能の低下が大きいという従来の問題点を排
除できる利点が得られる。さらに、巻線のセクシ
ヨン間ダクト内に凝縮液をジグ・ザグ状に流すと
ともに、その下流側に対向して流通孔を設けるよ
う構成した場合には、凝縮液の流れの径方向の分
力を増大させることができるので、蒸気気泡の排
出をより積極的に行うことができ、蒸気気泡によ
る耐電圧性能の低下をより一層効果的に阻止でき
る利点が得られる。 In addition, the flow velocity of the condensate in the axial passages on the winding side and the anti-winding side, which are communicated with each other through the flow holes, decreases on the winding side and increases on the anti-winding side as it goes downstream. It is possible to naturally generate the effect of sucking out steam bubbles to the axial passage side on the side opposite to the winding through the flow holes. Therefore, the closer the section coil is located in the upper position in the axial direction, the more easily the steam bubbles accumulate, and the more easily the steam bubbles accumulate. This provides the advantage of eliminating the conventional problem of large voltage performance drop. Furthermore, if the condensate is made to flow in a zig-zag pattern in the duct between sections of the winding, and a flow hole is provided on the downstream side of the duct, the radial component force of the flow of the condensate can be reduced. Therefore, it is possible to more actively discharge steam bubbles, and there is an advantage that deterioration of withstand voltage performance due to steam bubbles can be more effectively prevented.
第1図は本発明の実施例を示す側断面図、第2
図は蒸気気泡の状態を示す説明図、第3図は異な
る実施例を示す要部の側断面図、第4図は蒸気気
泡の状態を示す説明図、第5図は従来の散布形蒸
発冷却誘導電器の一例を示す側断面図、第6図は
セパレート形の一例を示す側断面図、第7図は従
来技術における蒸気気泡の状態を示す説明図であ
る。
1…タンク、2…鉄心、3…巻線、4…セクシ
ヨンコイル、5…絶縁容器、7…セクシヨン間ダ
クト、9…絶縁ガス、10…凝縮液、10C…高
電界部、10D…蒸気気泡、20…気泡を含んだ
凝縮液、21…循環ポンプ、25,35…密閉絶
縁容器、26…熱交換器、36,46…内側絶縁
容器、37,47…流通孔、38…軸方向通路
(巻線側)、39…軸方向通路(反巻線側)、31
A,31B…流量調整弁、22,23,32A,
32B…循環通路、33…連通管、49…液止
め。
FIG. 1 is a side sectional view showing an embodiment of the present invention, and FIG.
The figure is an explanatory diagram showing the state of steam bubbles, Figure 3 is a side sectional view of the main part showing a different embodiment, Figure 4 is an explanatory diagram showing the state of steam bubbles, and Figure 5 is conventional scattering type evaporative cooling. FIG. 6 is a side sectional view showing an example of an induction electric appliance, FIG. 6 is a side sectional view showing an example of a separate type, and FIG. 7 is an explanatory diagram showing the state of steam bubbles in the prior art. DESCRIPTION OF SYMBOLS 1... Tank, 2... Iron core, 3... Winding wire, 4... Section coil, 5... Insulating container, 7... Duct between sections, 9... Insulating gas, 10... Condensate, 10C... High electric field part, 10D... Steam bubble , 20... Condensate containing bubbles, 21... Circulation pump, 25, 35... Sealed insulating container, 26... Heat exchanger, 36, 46... Inner insulating container, 37, 47... Distribution hole, 38... Axial passage ( winding side), 39...Axial passage (counter-winding side), 31
A, 31B...Flow rate adjustment valve, 22, 23, 32A,
32B...Circulation passage, 33...Communication pipe, 49...Liquid stopper.
Claims (1)
したタンク内に収納され鉄心に巻装された巻線、
ならびにこの巻線を包囲収納するとともに循環通
路を介して前記熱交換器に連通した密閉絶縁容器
を備え、この密閉絶縁容器および熱交換器を循環
する絶縁媒体の凝縮液により前記巻線を冷却する
ものにおいて、前記密閉絶縁容器の内側に密閉絶
縁容器および前記巻線との間にそれぞれ軸方向通
路を保持するよう配設され連通管を介して前記熱
交換器に連通するよう形成された内側絶縁容器、
ならびにこの内側絶縁容器の側板に前記密閉絶縁
容器に連通するよう分布して形成された複数の導
液孔と、前記循環通路および連通管に設けられた
流量調整弁とを備えたことを特徴とする蒸発冷却
誘導電器。 2 特許請求の範囲第1項記載のものにおいて、
巻線が平板リング状のセクシヨンコイルとセクシ
ヨン間ダクトの層状組立体からなり、複数のセク
シヨンコイル毎にセクシヨンコイルの内径側外径
側交互に液止めを備え、セクシヨン間ダクトをジ
グ・ザグ状に流れる凝縮液の下流側に対向する部
分の内側密閉容器の側板に分布して連通孔が設け
られたことを特徴とする蒸発冷却誘導電器。 3 特許請求の範囲第1項記載のものにおいて、
循環通路および連通管それぞれに設けられた流量
調整弁が誘導電器の負荷情報検知手段の出力信号
により制御されることを特徴とする蒸発冷却誘導
電器。[Claims] 1. A winding wire wound around an iron core and housed in a tank having an external heat exchanger and containing insulating gas;
and a hermetically sealed insulating container that surrounds and accommodates this winding and communicates with the heat exchanger via a circulation passage, and the winding is cooled by a condensed liquid of an insulating medium that circulates through the hermetically insulated container and the heat exchanger. An inner insulator disposed inside the hermetically insulating container so as to maintain an axial passage between the hermetically insulating container and the winding, respectively, and communicating with the heat exchanger via a communication pipe. container,
The inner insulating container also includes a plurality of distributed liquid guide holes formed in the side plate thereof so as to communicate with the sealed insulating container, and a flow rate regulating valve provided in the circulation passage and the communication pipe. Evaporative cooling induction appliances. 2. In what is stated in claim 1,
The winding consists of a layered assembly of a flat ring-shaped section coil and an inter-section duct, and each of the plurality of section coils is provided with liquid stoppers alternately on the inner and outer diameter sides of the section coil. An evaporative cooling induction electric appliance characterized in that communication holes are provided distributed in a side plate of an inner sealed container in a portion facing the downstream side of a condensate flowing in a zigzag shape. 3 In what is stated in claim 1,
1. An evaporative cooling induction electric appliance, characterized in that a flow rate regulating valve provided in each of the circulation passage and the communication pipe is controlled by an output signal of a load information detection means of the induction electric appliance.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15746885A JPS6218014A (en) | 1985-07-17 | 1985-07-17 | Evaporative cooling induction electric apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15746885A JPS6218014A (en) | 1985-07-17 | 1985-07-17 | Evaporative cooling induction electric apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6218014A JPS6218014A (en) | 1987-01-27 |
| JPH0354846B2 true JPH0354846B2 (en) | 1991-08-21 |
Family
ID=15650329
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15746885A Granted JPS6218014A (en) | 1985-07-17 | 1985-07-17 | Evaporative cooling induction electric apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6218014A (en) |
-
1985
- 1985-07-17 JP JP15746885A patent/JPS6218014A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6218014A (en) | 1987-01-27 |
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