JPS6329806B2 - - Google Patents
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- Publication number
- JPS6329806B2 JPS6329806B2 JP56072670A JP7267081A JPS6329806B2 JP S6329806 B2 JPS6329806 B2 JP S6329806B2 JP 56072670 A JP56072670 A JP 56072670A JP 7267081 A JP7267081 A JP 7267081A JP S6329806 B2 JPS6329806 B2 JP S6329806B2
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- Prior art keywords
- firing
- molded body
- container
- temperature
- antimony oxide
- Prior art date
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Description
この発明は酸化亜鉛非直線抵抗素子成形体(以
下成形体と称す)を連続炉で焼成する際、酸化ア
ンチモンの蒸気と成形体を気一固相反応によつて
成形体の側面絶縁被膜を成形体の焼成と同時に成
形させる成形体の製造方法に関する。
従来より酸化亜鉛ZnOを主成分とする成形体は
非直線性が良好であるところから、例えば避雷器
用非直線抵抗体、即ち、特性要素として最適なも
のとなつているが、従来にあつてはその製造方法
が適当でなかつたことから、最終的に得られる成
形体のその側面には良好に絶縁被膜が形成され得
ないという欠点がある。
一般に上記成形体は例えば高純度酸化亜鉛
ZnO91mol%にSb2O3,Bi2O3,Co2O3MnO2,
SiO2,Cr2O3などを合計9mol%加えて混合、造
粒、圧縮成形した後特殊な雰囲気中で1000℃以上
1400℃以下の高温(電気的特性上からは1100℃〜
1300℃が適当であるとされている)下で焼成する
ことによつて得られる。この場合での特殊雰囲気
中での(本)焼成は成形体を焼成すると同時に、
その側面に高抵抗絶縁被膜を形成させるために必
要なものとなつている。しかしながら、本焼成の
ために加熱温度を徐々に上昇せしめる一次焼成
((仮焼)過程(この過程での800℃〜1000℃の温
度領域では成形体は体積比で40%程度収縮され
る)において、造粒過程で加えられた有機バイン
ダが熱分解され水分H2Oや酸化炭素CO2、水素
H2等の形で成形体外部に放出され、この放出さ
れたガスが成形体に作用して悪影響を与えるとい
うものである。ここにいう悪影響とは具体的には
放出ガスに含まれている還元性ガスあるいは高温
放出ガスより新たに生成された還元性ガスが本来
酸化物である成形体を還元することによつて生じ
る不具合を指している。また、一次焼成過程にお
いて有機バインダの熱分解が不十分であつてガス
の放出が不十分である場合には本焼成時にそれに
よる悪影響が現れ、成形体側面と成形された絶縁
被膜との間の密着性が良好でなく剥離し易かつた
り、均一性ある絶縁被膜が形成されないという不
具合がある。
ここで従来技術に係る焼成方法を説明すればこ
れは以下のようである。
即ち、第1図a,bは仮焼をほぼ密閉状態で行
なつた後、本焼成する場合を示す。第1図aに示
す如く焼成容器(アルミナ質)1内底面に台座
(アルミナ質あるいは酸化亜鉛系焼結板等の耐熱
性セラミツク材)6、敷粉(アルミナ質または成
形体の造粉末分あるいは仮焼成形体の破砕粉等)
5を介し成形体3を載置し、蓋(アルミナ質)4
によつて焼成容器1内部をほぼ密閉にした状態で
仮焼するものである。
仮焼後は第1図bに示すように例えば焼成容器
1内側面に絶縁被膜形成用の塗布剤(アンチモン
酸化物Sb2O3,Sb2O4,Sb2O5のうち少なくとも
何れか1つを含むもの、あるいはそのものを主成
分とする化合物)2を塗布し、塗布剤2の乾燥後
は蓋4によつて焼成容器1を密閉にした状態で仮
焼成形体3が本焼成されるようにしたものであ
る。尤も仮焼と本焼成を第1図bに示す如くにし
た状態で同一焼成容器で同時的に行なうようにす
ることも可能である。本焼成時には塗布剤2中に
含まれるアンチモン酸化物が920℃付近より昇華
し、1000℃以上では昇華は非常に活発となり焼成
容器内はアンチモン酸化物の雰囲気となり、これ
が非直線抵抗体の側面に作用することによつて側
面には高抵抗絶縁被膜であるスピネル(Zn2,33
Sb0.67O4)が形成されるものである。
ところで既述したように成形体を密閉状態の下
で仮焼することは好ましいものでないことは明ら
かであり、むしろ開放状態の下で仮焼するのが望
ましいと云える。第2図はそのための焼成容器を
示したものである。これによると、焼成容器は焼
成容器本体(アルミナ質)7と蓋(アルミナ質)
8とからなるが、焼成容器本体7の上部縁には切
欠部9が設けられていることから、蓋8によつて
焼成容器本体7内部を密閉状態にしようとしても
密閉状態におくことは不可能であることが従来の
ものと異なつている。
即ち、成形体は密閉状態で仮焼されなく、ガス
化した有機バインダは仮焼中切欠部9より焼成容
器本体7外に飛散し得るものである。
したがつて仮焼は第2図に示す焼成容器により
行なう一方、本焼成は第1図bに示す如くにして
行なうようにすれば、成形体の側面には状態良好
にして高抵抗絶縁被膜が形成されることになる。
しかしながら、仮焼と本焼成とに別個に高価な
焼成容器を要するということは経済的ではないば
かりか、仮焼と本焼成が同時的に行ない得ないと
いう新たな問題が生じる。尚、第2図に示す焼成
容器を用い本焼成をも行なう場合は成形体より
Bi2O3が飛散することから、最終的に得られる成
形体の電気的特性は良好ではなくなる。
この発明は上記の事情に鑑みてなされたもの
で、成形体の仮焼と本焼成とにそれぞれの用途の
焼成容器を用いることなく同一焼成容器を以て同
時的に仮焼と本焼成とが行ない得、しかも成形体
の側面には高抵抗絶縁被膜が状態良好にして形成
され得る成形体の製造方法を提供することを目的
とする。
以下図面を参照してこの発明の一実施例を説明
する。第3図a,bにおいて、第1図a,bと同
一部分は同一符号を付して示す。焼成容器1内部
は焼成容器本体16に蓋17が外側より嵌合され
ることによつて密閉されるが蓋17の焼成容器本
体16への嵌合の深さを浅くしておき、それによ
つて蓋17の下部内側面21と焼成容器本体16
の外側面との間に形成される空スペースにアンチ
モン酸化物22を介在させるものである。このア
ンチモン酸化物22に対向する焼成容器本体16
側面に穴18を穿つているのはその空スペースに
アンチモン酸化物22を収容させるためである。
また蓋17側面には焼成容器本体16の上端面に
一致する高さ位置から上方向に一定長さ穴19を
穿つようにするものである。
更に必要に応じ蓋17の下部内側面に溝20を
形成し、この溝20には、溝20に対向する焼成
容器本体16側面に穿たれた穴18を介しアンチ
モン酸化物22を収容せしめるものである。
したがつて、成形体3を収容せしめた図示の状
態より後述の連続電気炉の焼成温度を徐々に上昇
せしめるようにすれば、空スペースに収容された
アンチモン酸化物22は溝20内に収容されたア
ンチモン酸化物ともども昇華により徐々にその量
が減少するところとなり、それに伴れて蓋17が
自重により徐々に下降し嵌合が深くなつていくわ
けである。よつて予め空スペースの上下方向にお
ける長さが穴19のそれよりも大であるようにし
ておけば、仮焼時にはガス化有機バインダが穴1
9を介して外部に逃げ得、また本焼成が行なわれ
る時分には穴19は完全に焼成容器本体16側面
によつて閉塞され、この密閉状態ではアンチモン
酸化物22による昇華アンチモン酸化物の雰囲気
中で本焼成が行ない得るものである。
上記実施例のように形成された焼成容器本体1
6は第4図に示す連続電気炉25の移動台26上
に所定の間隔をおいて載置され、焼成容器本体1
6の焼成を行なう。このときの焼成パターンは第
5図に示すように行なわれる。すなわち、第5図
において、横軸には炉長あるいは時間を、縦軸に
は温度をとつてあり、移動台26に載置された焼
成容器本体16は徐々に炉25内の温度が上昇さ
れるので、これに伴つて徐々に加熱(仮焼)され
る。この加熱により成形体3に用いた有機バイン
ダーは分解蒸発し、その蒸気は炉の温度が800℃
位になるまでに前述したように穴19から焼成容
器本体16の外部に逃げてしまう。その後、炉内
が約850℃に達すると成形体3は第6図に示すよ
うに収縮され始め、920℃になるとアンチモン酸
化物22が昇華され始まる。さらに炉内の温度を
上昇させると成形体3は充分収縮され、炉内の温
度を950℃〜1150℃のうち所定の温度に保つて約
1時間から10時間の間その温度を維持させたまま
とする。前記920℃で昇華され始まつたアンチモ
ン酸化物22は温度上昇とともに活発化される。
一方前述したように蓋17が自重により徐々に下
降し、穴19が蓋17により閉塞されるため、焼
成容器本体16内はアンチモン酸化物蒸気で満さ
れる。このため、成形体3の側面の酸化亜鉛とア
ンチモン酸化物蒸気とが気一固相反応によつて成
形体3の側面に絶縁被膜、すなわち、スピネル
(Zn7Sb3O12)が成形される。第5図でA領域と
して示してあるのが温度を950℃〜1150℃のうち
所定の温度に保つ時間である。
上記のようにして成形体3の側面に絶縁被膜を
成形させることにより緻密な被膜が得られる。被
膜成形後、B領域まで温度を上昇させて本焼成を
行なう。このときの温度は1160℃〜1300℃に設定
する。
次表は焼成温度を950℃〜1150℃、焼成時間を
1時間〜10時間に設定して製造した成形体の放電
耐量(4×10μs)の実験結果である。
なお、成形体は40φ×38t、電流は30KA〜
70KA 1分間隔で2回供給した場合である。○
印は異常なし、×印は沿面閃絡を示す。
In this invention, when firing a zinc oxide nonlinear resistance element molded body (hereinafter referred to as a molded body) in a continuous furnace, an insulating coating on the side surface of the molded body is formed by a gas-solid reaction between antimony oxide vapor and the molded body. The present invention relates to a method for producing a molded body, which is formed at the same time as the body is fired. Conventionally, molded bodies containing zinc oxide ZnO as a main component have good nonlinearity, so they have become optimal as nonlinear resistors for lightning arresters, that is, as characteristic elements. Since the manufacturing method was not appropriate, there is a drawback that an insulating coating cannot be formed satisfactorily on the side surface of the molded product finally obtained. Generally, the above molded body is made of high purity zinc oxide, for example.
ZnO91mol% Sb 2 O 3 , Bi 2 O 3 , Co 2 O 3 MnO 2 ,
After adding a total of 9 mol% of SiO 2 , Cr 2 O 3 , etc., mixing, granulating, and compression molding, it is heated at 1000℃ or higher in a special atmosphere.
High temperature below 1400℃ (1100℃~ from electrical characteristics)
It is obtained by firing at a temperature of 1300°C (which is said to be appropriate). In this case, (actual) firing in a special atmosphere is performed at the same time as firing the molded body.
This is necessary to form a high-resistance insulating coating on the side surface. However, in the primary firing ((calcination) process in which the heating temperature is gradually raised for main firing (in this process, the compact shrinks by about 40% in terms of volume) in the temperature range of 800℃ to 1000℃. , the organic binder added during the granulation process is thermally decomposed to produce water H 2 O, carbon oxide CO 2 , and hydrogen.
The gas is released to the outside of the molded product in the form of H2, etc., and this released gas acts on the molded product and has an adverse effect. Specifically, the adverse effects referred to here are problems caused by the reducing gas contained in the emitted gas or the reducing gas newly generated from the high temperature emitted gas reducing the molded product, which is originally an oxide. is pointing to. Additionally, if the thermal decomposition of the organic binder is insufficient during the primary firing process and the release of gas is insufficient, this will have an adverse effect during the main firing process, causing damage between the side surface of the molded body and the molded insulating coating. Problems include poor adhesion, easy peeling, and failure to form a uniform insulating film. Here, the firing method according to the prior art will be explained as follows. That is, FIGS. 1a and 1b show the case where the main firing is performed after the calcination is performed in a substantially closed state. As shown in FIG. crushed powder of calcined compacts, etc.)
Place the molded body 3 through the lid (alumina) 4.
Calcination is performed in a state in which the inside of the firing container 1 is substantially sealed. After calcination, as shown in FIG. 1b, for example, a coating agent for forming an insulating film (at least one of antimony oxides Sb 2 O 3 , Sb 2 O 4 , and Sb 2 O 5 ) is applied to the inner surface of the firing container 1. After the coating agent 2 has dried, the calcined compact 3 is fired with the firing container 1 sealed with the lid 4. This is what I did. Of course, it is also possible to carry out the calcination and main firing simultaneously in the same firing container in the state shown in FIG. 1b. During the main firing, the antimony oxide contained in coating agent 2 sublimates from around 920°C, and at temperatures above 1000°C, the sublimation becomes very active, creating an atmosphere of antimony oxide inside the firing container, which spreads onto the sides of the nonlinear resistor. As a result of this action, spinel (Zn 2,33
Sb 0 . 67 O 4 ) is formed. By the way, as mentioned above, it is clear that it is not preferable to calcinate the molded body under a closed condition, and it can be said that it is rather desirable to calcinate the molded body under an open condition. FIG. 2 shows a firing container for this purpose. According to this, the firing container consists of a firing container body (alumina) 7 and a lid (alumina).
However, since the upper edge of the firing container body 7 is provided with a notch 9, even if the inside of the firing container body 7 is tried to be sealed with the lid 8, it will not be possible to keep it in a sealed state. What is possible is different from conventional ones. That is, the compact is not calcined in a sealed state, and the gasified organic binder may be scattered outside the firing container main body 7 through the notch 9 during calcining. Therefore, if the calcination is carried out in the sintering container shown in Fig. 2, and the main sintering is carried out as shown in Fig. 1b, the sides of the molded body will be in good condition and a high-resistance insulating coating will be formed. will be formed. However, not only is it not economical to require separate expensive firing containers for calcination and main firing, but also a new problem arises in that calcination and main firing cannot be performed simultaneously. In addition, if you also perform the main firing using the firing container shown in Figure 2,
Since Bi 2 O 3 is scattered, the electrical properties of the final molded product are not good. This invention was made in view of the above circumstances, and it is possible to simultaneously perform calcination and main firing of a molded body in the same firing container without using separate firing containers for each purpose. Moreover, it is an object of the present invention to provide a method for producing a molded body in which a high-resistance insulating coating can be formed on the side surface of the molded body in good condition. An embodiment of the present invention will be described below with reference to the drawings. In FIGS. 3a and 3b, the same parts as in FIGS. 1a and 1b are designated by the same reference numerals. The inside of the firing container 1 is sealed by fitting the lid 17 to the firing container main body 16 from the outside, but the depth of the fitting of the lid 17 to the firing container main body 16 is made shallow. Lower inner surface 21 of lid 17 and firing container body 16
The antimony oxide 22 is interposed in the empty space formed between the outer surface of the substrate and the outer surface of the substrate. Firing container body 16 facing this antimony oxide 22
The reason why the hole 18 is bored in the side surface is to accommodate the antimony oxide 22 in the empty space.
Further, a hole 19 having a certain length is bored in the side surface of the lid 17 upward from a height that corresponds to the upper end surface of the firing container body 16. Furthermore, if necessary, a groove 20 is formed on the inner surface of the lower part of the lid 17, and the antimony oxide 22 is accommodated in this groove 20 through a hole 18 bored in the side surface of the firing container body 16 opposite to the groove 20. be. Therefore, if the firing temperature of the continuous electric furnace, which will be described later, is gradually increased from the illustrated state in which the compact 3 is accommodated, the antimony oxide 22 accommodated in the empty space will be accommodated in the groove 20. The amount of the antimony oxide and other antimony oxide gradually decreases due to sublimation, and as a result, the lid 17 gradually descends due to its own weight and the fitting becomes deeper. Therefore, if the length of the empty space in the vertical direction is set in advance to be larger than that of the hole 19, the gasified organic binder will fit into the hole 1 during calcination.
At the time of main firing, the hole 19 is completely closed by the side surface of the firing container main body 16, and in this sealed state, an atmosphere of sublimated antimony oxide by the antimony oxide 22 is released. The main firing can be carried out inside. Firing container body 1 formed as in the above embodiment
6 are placed at predetermined intervals on a moving table 26 of a continuous electric furnace 25 shown in FIG.
Perform step 6 of firing. The firing pattern at this time is as shown in FIG. That is, in FIG. 5, the furnace length or time is plotted on the horizontal axis, and the temperature is plotted on the vertical axis. As a result, it is gradually heated (calcined). Due to this heating, the organic binder used in the molded body 3 decomposes and evaporates, and the vapor reaches a temperature of 800℃ in the furnace.
As described above, the particles escape to the outside of the firing container main body 16 through the holes 19. Thereafter, when the temperature inside the furnace reaches approximately 850°C, the compact 3 begins to shrink as shown in FIG. 6, and when the temperature reaches 920°C, the antimony oxide 22 begins to sublimate. When the temperature inside the furnace is further increased, the compact 3 is sufficiently shrunk, and the temperature inside the furnace is maintained at a predetermined temperature between 950°C and 1150°C for about 1 to 10 hours. shall be. The antimony oxide 22 that started to sublimate at 920°C becomes activated as the temperature rises.
On the other hand, as described above, the lid 17 gradually descends due to its own weight and the hole 19 is closed by the lid 17, so that the inside of the firing container body 16 is filled with antimony oxide vapor. For this reason, an insulating coating, that is, spinel (Zn 7 Sb 3 O 12 ) is formed on the side surface of the molded body 3 through a gas-solid phase reaction between zinc oxide and antimony oxide vapor on the side surface of the molded body 3. . The area A in FIG. 5 is the time period during which the temperature is maintained at a predetermined temperature within the range of 950°C to 1150°C. By forming an insulating coating on the side surface of the molded body 3 as described above, a dense coating can be obtained. After forming the film, the temperature is raised to region B and main firing is performed. The temperature at this time is set at 1160°C to 1300°C. The following table shows the experimental results of the discharge withstand capacity (4 x 10 μs) of molded bodies manufactured by setting the firing temperature to 950° C. to 1150° C. and the firing time to 1 hour to 10 hours. The molded body is 40φ x 38t, and the current is 30KA~
This is the case where 70KA is supplied twice at 1 minute intervals. ○
The mark indicates no abnormality, and the mark x indicates creeping flash.
【表】
上述の実験結果から明らかのように成形体3の
側面に緻密な絶縁被膜が成形され、しかも放電耐
量が実用的になる焼成温度は950℃〜1150℃、焼
成時間は1時間から10時間となる。
第7図は成形体3の側面に特に均一な絶縁被膜
を形成させる必要がある場合の実施例で、この第
7図においては孔24が多数穿たれてなる板材
(アルミナ質)23を、穴18を囲むようにして
焼成容器本体16内部に配設する。このように板
材23を用いれば、穴18からの昇華アンチモン
酸化物22は適当に板材23によつて拡散された
状態で成形体3の側面と気一固相反応するように
なる。
なお、アンチモン酸化物中に予めBi2O3を含ま
せておく場合は、焼成中成形体からのBi2O3の飛
散を防止することが可能である。
以上述べたようにこの発明によれば、連続炉内
において予め焼成容器内にアンチモン酸化物を介
在させておき、その酸化物が蒸気になるに従つて
容器内が密閉状態となるようにし、かつ炉内の温
度を950℃〜1150℃に保持して1時間から10時間
のうち、任意時間容器を焼成させるようにしたの
で、有機バインダが焼成容器外部に放出された後
には容器内がアンチモン酸化物蒸気で満されるた
めに成形体の側面に均一な絶縁被膜が成形され
る。また、その被膜成形が気一固相反応により行
なわれるので、緻密な被膜が得られ、かつ沿面閃
絡の向上を図ることができる。
さらに、従来に比較して絶縁材塗料を作る工程
と塗布乾燥工程が省略でき、作業能率が飛躍的に
向上する等の効果がある。[Table] As is clear from the above experimental results, the firing temperature at which a dense insulating film is formed on the side surface of the compact 3 and the discharge resistance is practical is 950°C to 1150°C, and the firing time is from 1 hour to 10 It's time. FIG. 7 shows an example in which it is necessary to form a particularly uniform insulating coating on the side surface of the molded body 3. In this FIG. It is arranged inside the firing container body 16 so as to surround the firing container body 18 . By using the plate material 23 in this manner, the sublimated antimony oxide 22 from the hole 18 is appropriately diffused by the plate material 23 and reacts with the side surface of the molded body 3 in a gas-solid state. Note that when Bi 2 O 3 is included in the antimony oxide in advance, it is possible to prevent Bi 2 O 3 from scattering from the compact during firing. As described above, according to the present invention, antimony oxide is interposed in advance in the firing container in a continuous furnace, and as the oxide becomes vapor, the inside of the container becomes airtight. Since the temperature inside the furnace was maintained at 950°C to 1150°C and the container was fired for an arbitrary period of time from 1 hour to 10 hours, antimony oxidation occurred inside the container after the organic binder was released to the outside of the firing container. A uniform insulating coating is formed on the sides of the molded body because it is filled with vapor. Furthermore, since the coating is formed by a gas-solid phase reaction, a dense coating can be obtained and creeping flash resistance can be improved. Furthermore, compared to the conventional method, the process of making an insulating paint and the process of applying and drying can be omitted, resulting in a dramatic improvement in work efficiency.
第1図a,bは従来技術に係る焼成方法を説明
するための図、第2図は従来技術に係る焼成方法
の実施に際して使用される仮焼用焼成容器の説明
図、第3図a,bはこの発明の実施例に使用され
る焼成容器の一部省略断面図と側面図、第4図は
焼成容器を連続炉で焼成する場合の既略的な説明
図、第5図は第4図の連続炉における焼成パター
ンを示す特性図、第6図は成形体の体積収縮率を
示す特性図、第7図はこの発明の他の実施例とし
て適用される焼成容器の一部省略断面図である。
1……焼成容器、3……成形体、16……焼成
容器本体、17……蓋、18,19……穴、20
……溝、22……アンチモン酸化物、25……連
続電気炉、26……移動台。
1a and 1b are diagrams for explaining the firing method according to the prior art, FIG. b is a partially omitted cross-sectional view and side view of a firing container used in an embodiment of the present invention, FIG. 4 is a schematic explanatory diagram when the firing container is fired in a continuous furnace, and FIG. Fig. 6 is a characteristic diagram showing the firing pattern in the continuous furnace shown in Fig. 6; Fig. 6 is a characteristic diagram showing the volumetric shrinkage rate of the compact; Fig. 7 is a partially omitted sectional view of a firing container applied as another embodiment of the present invention. It is. 1... Baking container, 3... Molded body, 16... Baking container body, 17... Lid, 18, 19... Hole, 20
... Groove, 22 ... Antimony oxide, 25 ... Continuous electric furnace, 26 ... Moving table.
Claims (1)
化亜鉛非直線抵抗素子成形体を焼成する際、予め
焼成容器内にアンチモン酸化物を介在させてお
き、そのアンチモン酸化物が蒸気になるに従つて
容器内が次第に密閉状態となるようにし、かつ前
記炉の温度を950℃〜1150℃に保持するとともに
その保持時間を1時間から10時間のうち所定時間
に設定して焼成し、前記容器内の成形体の側面に
気一固相反応によりスピネル絶縁被膜を成形させ
た後、前記炉の温度を上昇させて本焼成を行うこ
とを特徴とする酸化亜鉛非直線抵抗素子成形体の
製造方法。1. In a continuous furnace, when firing a zinc oxide nonlinear resistance element molded body housed in a firing container, antimony oxide is interposed in the firing container in advance, and as the antimony oxide becomes vapor, The inside of the container is gradually closed, and the temperature of the furnace is maintained at 950°C to 1150°C, and the holding time is set to a predetermined time of 1 to 10 hours for firing. A method for manufacturing a zinc oxide nonlinear resistance element molded body, which comprises forming a spinel insulating coating on the side surface of the molded body by gas-solid phase reaction, and then performing main firing by increasing the temperature of the furnace.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56072670A JPS57187909A (en) | 1981-05-14 | 1981-05-14 | Method of producing zinc oxide nonlinear resistance element former |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56072670A JPS57187909A (en) | 1981-05-14 | 1981-05-14 | Method of producing zinc oxide nonlinear resistance element former |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57187909A JPS57187909A (en) | 1982-11-18 |
| JPS6329806B2 true JPS6329806B2 (en) | 1988-06-15 |
Family
ID=13496019
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56072670A Granted JPS57187909A (en) | 1981-05-14 | 1981-05-14 | Method of producing zinc oxide nonlinear resistance element former |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57187909A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110156454A (en) * | 2019-05-27 | 2019-08-23 | 国网湖南省电力有限公司 | The preparation method of zinc oxide varistor |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5778105A (en) * | 1980-10-31 | 1982-05-15 | Meidensha Electric Mfg Co Ltd | Method of producing voltage nonlinear resistor |
-
1981
- 1981-05-14 JP JP56072670A patent/JPS57187909A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110156454A (en) * | 2019-05-27 | 2019-08-23 | 国网湖南省电力有限公司 | The preparation method of zinc oxide varistor |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57187909A (en) | 1982-11-18 |
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