JPH0360163B2 - - Google Patents

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Publication number
JPH0360163B2
JPH0360163B2 JP57181011A JP18101182A JPH0360163B2 JP H0360163 B2 JPH0360163 B2 JP H0360163B2 JP 57181011 A JP57181011 A JP 57181011A JP 18101182 A JP18101182 A JP 18101182A JP H0360163 B2 JPH0360163 B2 JP H0360163B2
Authority
JP
Japan
Prior art keywords
zinc oxide
nonlinear resistor
manufacturing
voltage nonlinear
water
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 - Lifetime
Application number
JP57181011A
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Japanese (ja)
Other versions
JPS5968907A (en
Inventor
Yoshio Takada
Tomoji Morita
Ken Sato
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Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric Corp
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
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Application filed by Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP57181011A priority Critical patent/JPS5968907A/en
Publication of JPS5968907A publication Critical patent/JPS5968907A/en
Publication of JPH0360163B2 publication Critical patent/JPH0360163B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

この発明は避雷器、サージ吸収器に使用され
る、酸化亜鉛を主成分とする電圧非直線抵抗体の
製造方法に関するものである。 従来、酸化亜鉛電圧非直線抵抗体を製造する場
合、一般的には主成分の酸化亜鉛をはじめ酸化ビ
スマス、酸化コバルトなどの添加物も酸化物粉末
原材料として使用する。これら各種の粉末は水を
加えボールミル等の手段で混合され、乾燥後適当
なバインダを加えて顆粒をつくり、プレス成形を
経て1200℃前後の温度で焼成して焼結体を得る。
これに研磨電極の形成ののち素子が得られる。こ
れらの工程中、顆粒を形成する造粒工程は大量生
産の場合、PVA(ポリビニールアルコール)など
のバインダを加えた泥漿をトルネードリアクタ、
スプレイドライヤ等の乾燥装置を使つて乾燥顆粒
を造ることがよく行われている。 電圧非直線抵抗体の種々の電気特性は、製造方
法及びその製造パラメータにより大きく変化する
ことは周知の通りである。例えば、混合工程の場
合、主成分以外の微量添加物が10種類近くあるこ
と、各粉末密度がかなり異なること(酸化亜鉛密
度:5.6g/cm3、酸化ビスマス密度:8.9g/cm3
酸化珪素密度:2.2g/cm3等)などの理由により
十分均一な混合をするにはかなり困難な点があつ
た。混合不良はセラミツク自体の均一性を悪化さ
せ、ひいては電圧非直線性、寿命、各種耐量試験
不良などとしてあらわれる。 混合の均一性の確保に関する言及は少ないが、
例えば特開昭48−97090号公報に記載されている
ような添加物イオン水溶液を酸化亜鉛粉末に加
え、混合するという方法が提案されている。この
混合物はミクロな意味でよく混合しており、得ら
れた焼結体は通常の粉末を出発原料としたものと
比較すると、粒子径もよく揃い欠陥も少なくしか
も電流−電圧特性、寿命特性などもすぐれてい
る。 これらの塩を混合する方法は、素子にすぐれた
特性を付与するが、実際の製作過程では泥漿の乾
燥方式の点で問題のあることがわかつた。 これについて若干述べる。第1図に、酸化亜鉛
を主成分とする電圧非直線抵抗体の微細構造模型
を示す。図中、抵抗体の微細構造は酸化亜鉛を主
成分とする粒子1、主として酸化ビスマスを主成
分とする境界層2、酸化アンチモンを添加した場
合に生じるスピネル等の粒子3を含む。電圧非直
線性が発生する根源は、酸化亜鉛粒子同志、又は
酸化亜鉛及び酸化ビスマスの境界層に存在する電
気的な障壁に関連するものであると考えられてい
る。障壁にかかる電圧の大小により、(1)オーミツ
ク領域、(2)シヨツトキ領域、(3)トンネル領域、及
び(4)酸化亜鉛粒子の抵抗が電流−電圧特性を支配
する領域とにわかれる。避雷器の場合には課電条
件にもよるが、もれ電流領域はほぼ(2)に相当しい
わゆる制限電圧と定義される電流領域(10KA−
20KA)は(3)及び(4)に相当する。すなわち、保護
特性のすぐれた素子は(2)の領域における電流安定
性(寿命)がよく、(3)ないしは(4)に関係する制限
電圧ができる限り小さい方が望ましい。 今迄の微細構造の検討及び反応メカニズムの検
討から、酸化ビスマス(又は高温で酸化ビスマス
になるような化合物例えば硝酸ビスマスなど)
は、焼成時には液相となり、酸化亜鉛粒子の結晶
成長を促進し、クロム等のイオンを固溶し、酸化
亜鉛粒子をおおうように存在する。コバルト、ニ
ツケル、マンガン、クロム、アルミニウムなどの
イオンは酸化亜鉛粒子に固溶するが、一部は酸化
アンチモン(もしくは高温で分解し酸化アンチモ
ンとなるもの例えば酒石酸アンチモン)とももに
スピネル粒子を形成する。これから、酸化亜鉛粒
子内に固溶する成分は主として大電流領域(前記
(3)及び(4))に関連し、酸化ビスマスなどのように
酸化亜鉛と容易に反応せず、粒子間に存在するも
のについては主として低電流領域(前記(1)及び
(2))に関係する。なお、第2相のスピネル粒子は
酸化亜鉛部分、酸化ビスマス部分への各種イオン
の分配に関与していると考えられる。 さて、各種の塩の水溶液の作成にあたり、ニツ
ケル、コバルト、マンガン及びクロムなどの硝酸
塩は水によく溶解し、また酒石酸アンチモンも易
溶性である。一方、ビスマスの硝酸塩は水には不
溶性で水酸化物状態の白沈を生じるが、これに濃
硝酸を添加してPHを小さくすることにより白沈は
消滅し均一に溶解する。十分に濃い硝酸々性中で
ビスマスイオンは安定に存在するが、この溶液を
多量の酸化亜鉛粉末と反応させると、次式に従い
硝酸は酸化亜鉛とすみやかに反応するため、 ZoO+2HNO3→Zo(NO32+H2O 溶液のPHは大きくなりビスマスイオンはただち
に白沈を形成する。すなわち、硝酸を含む硝酸ビ
スマスの水溶液はみかけ上一様な水溶液である
が、この水溶液を酸化亜鉛粉末と混合するとすぐ
に白沈し固相を形成するため、他の添加イオン成
分との混合と同様には扱えず、均一な分散性にも
問題を生じる。 特にこれらの泥漿を静置して乾燥すると、ビス
マスイオン以外は水溶液の蒸発乾固物となるが、
ビスマスは白沈物として固相から乾燥されること
になり、しかもこの密度が極めて大きいことから
ビスマスに関しては均一性の高い乾燥粉末を得る
ことが極めて困難となり、これが低電流側の電流
電圧特性を悪化させ、寿命特性にも悪影響を与え
ることがわかつた。 なお、ここで硝酸ビスマスの使用を主としての
べてきたが塩酸ビスマスをアルコール溶液で使用
した場合にも水が多量にあると容易に加水分解を
起し同相を形成するので同様である。 いずれにしても、ビスマスイオンに関しては溶
液状態で酸化亜鉛と混合することは困難であるた
め、この白沈物が生じてもできるだけよりよい混
合状態で乾燥させる必要がある。こうすれば他の
添加イオンの分散性はもともと良好なため、全体
的に均一性が向上し、低電流側の電流電圧特性も
大巾に改善されることがわかつた。 ここで量産性を考慮し、しかもできるだけ各元
素が均一に混合された状態で乾燥が可能であるこ
とを条件として種々検討した結果、噴霧乾燥器を
使用する方法が望ましいことがわかつた。しかも
従来実施されているような水溶性バインダを加え
ておくことにより球状の顆粒が得られ、さらに比
較的高温度で乾燥されるため、各種塩も分解され
やすいものを使用しておけば塩の熱分解工程も不
用であるなどの有利な点もあることがわかつた。 この発明は以上のような知見に基いてなされた
ものであり、酸化亜鉛を主成分とした電圧非直線
抵抗体を製造する方法において、酸化亜鉛粉末、
添加物の金属塩水溶液、添加物の一部の沈澱物及
び水溶液バインダを含む混合泥漿を撹拌又は擾乱
により均一化し、該混合泥漿を連続的に噴霧乾燥
し、前記酸化亜鉛粉末以外の沈澱物及び各種塩の
分解及び酸化と、顆粒の形成とを同時に行なう電
圧非直線低抗体の製造方法に存する。 上記混合泥漿は好適には酸化亜鉛、添加物塩水
溶液、及び水溶性バインダを含む泥漿に最終的に
濃硝酸を含むビスマスイオン溶液を加えて製造す
る。 また、金属塩は噴霧乾燥時に分解する化合物で
硝酸塩及び酒石酸塩のいずれかが好適に使用でき
る。噴霧乾燥時の熱風温度は好適には金属塩の分
解に必要な温度で、かつ水溶性バインダを分解し
ない温度に設定する。 以下にプロトタイプの実験の実施例に沿つて本
発明を説明する。 実施例 第2図に一例として二流体ノズル方式の噴霧乾
燥器の場合の混合造粒過程の概略図を示した。図
中、デイスパーミル4で製造した泥漿は泥漿輸送
用ポンプ6によりコンプレツサ10(二流体ノズ
ルの場合)の圧縮空気と共に噴霧乾燥器本体6内
のノズル11から噴霧される。加熱器7を通つた
空気は噴霧乾燥器本体(加熱塔)本体6に入りノ
ズル11から飛来する霧を瞬時に乾燥させ、乾燥
粉を顆粒取り出し口12から取り出す。 混合泥漿の調製は以下のように行なう。デイス
パーミル内に水を1.5程度入れ、更に3%PVA
溶液2、界面活性剤2%水溶液1及び消泡剤
20c.c.を入れあらかじめ混合しておく。次に硝酸ニ
ツケル、硝酸コバルト、硝酸クロム、硝酸アルミ
ニウムを所定量秤量し全体1.0の水に溶解して
おく(第1液)。次にやはり所定量の酸化アンチ
モンを酒石酸水溶液に溶解して第2液0.3をつ
くり、硝酸ビスマスを水200c.c.と濃硝酸100c.c.の混
合溶液に溶かし第3液をつくつてビーカに準備し
ておく。 第1液及び第2液を全量デイスパーミル内に投
入して約15分混合後、これに酸化亜鉛粉末10Kgを
ゆつくり(全量を約10分程度かけて)混入し、約
1時間混合運転をする。最後に第3液を約5分位
かけてゆつくり混入し、その後15分程度全体で1
〜1.5時間位混合する。この混合泥漿をポンプで
噴霧乾燥器に連続的に供給する。噴霧乾燥器の運
転条件は熱風温度約250℃、排風温度120℃、噴霧
圧1.0Kg/cm2、吐出圧0.8Kg/cm2である。 この泥漿量では約15分程度で乾燥は完了し、乾
燥塔下部より粉末をとり出す。得られた粉末の粒
度分布としては150μ以上:40%、100〜150μ:40
%、100〜50μ:20%程度であり、粉末混合品と
ほとんど違わない。流れ性はほぼ粉末混合品と同
様で、カサ密度は1.2.g/cm3とやや小さかつた。
顕微鏡観察では形状もほぼ球状で若干連鎖球その
他の異形もあつた。 この造粒粉々末の一部を熱天秤などで調べる
と、水およびPVA、界面活性剤の分解によると
思われる重量減少が〜600℃付近迄に観察される
が、硝酸塩分解によると思われる特別な反応はみ
られず、噴霧乾燥時点ではほとんど分解が完了し
てしまつていると考えられる。それ故特別な熱分
解工程も不用であることがわかつた。 得られた粉末を使用し、通常の一軸性成形器で
300Kg/cm2の加圧力でプレスし、1200℃で4時間
焼成した後研磨電極づけをおこない電流電圧特性
を調べた(これをA試料とする)。各種塩溶液、
ビスマス沈澱物、酸化亜鉛粉末泥漿をバツチ式の
静置乾燥方法をとつた後、全く同様なプロセスで
素子をつくつた場合をB試料、粉末混合品をC試
料とする。 これらA,B及びC試料の収縮率を調べたこと
ころ表のような結果となり、明らかにA試料及び
B試料は粉末混合C試料よりよく収縮しており、
均一な反応焼結が起つていることがうかがい得
る。なお、酸化亜鉛粒子径はA,B及びC試料で
ほぼ15μmで一定であつた。
The present invention relates to a method for manufacturing a voltage nonlinear resistor containing zinc oxide as a main component and used in lightning arresters and surge absorbers. Conventionally, when manufacturing a zinc oxide voltage nonlinear resistor, the main component, zinc oxide, and additives such as bismuth oxide and cobalt oxide are generally used as oxide powder raw materials. These various powders are mixed by adding water and using a ball mill or other means, and after drying, a suitable binder is added to form granules, which are then press-molded and fired at a temperature of around 1200°C to obtain a sintered body.
After forming a polished electrode on this, an element is obtained. Among these processes, in the granulation process to form granules, in the case of mass production, slurry with a binder such as PVA (polyvinyl alcohol) is added to a tornado reactor,
Dry granules are often produced using drying equipment such as spray dryers. It is well known that the various electrical characteristics of voltage nonlinear resistors vary greatly depending on the manufacturing method and manufacturing parameters. For example, in the case of the mixing process, there are nearly 10 types of trace additives other than the main ingredients, and the density of each powder is quite different (zinc oxide density: 5.6 g/cm 3 , bismuth oxide density: 8.9 g/cm 3 ,
Due to reasons such as silicon oxide density: 2.2 g/cm 3 etc., it was quite difficult to achieve sufficiently uniform mixing. Poor mixing deteriorates the uniformity of the ceramic itself, which in turn appears as voltage nonlinearity, failure in life, and failure in various durability tests. Although there is little mention of ensuring uniformity of mixing,
For example, a method has been proposed in which an aqueous additive ion solution is added to zinc oxide powder and mixed, as described in JP-A-48-97090. This mixture is well mixed in a microscopic sense, and the resulting sintered body has a well-uniformed particle size and fewer defects, as well as current-voltage characteristics and life characteristics, compared to those using ordinary powder as a starting material. It's also excellent. Although the method of mixing these salts gives the device excellent properties, it has been found that there are problems in the drying method of the slurry in the actual manufacturing process. I will say a few words about this. FIG. 1 shows a microstructure model of a voltage nonlinear resistor whose main component is zinc oxide. In the figure, the fine structure of the resistor includes particles 1 mainly composed of zinc oxide, a boundary layer 2 mainly composed of bismuth oxide, and particles 3 of spinel or the like produced when antimony oxide is added. The source of voltage nonlinearity is thought to be related to electrical barriers existing between zinc oxide particles or in a boundary layer between zinc oxide and bismuth oxide. Depending on the magnitude of the voltage applied to the barrier, it can be divided into (1) an ohmic region, (2) a shot region, (3) a tunnel region, and (4) a region where the resistance of zinc oxide particles controls the current-voltage characteristics. In the case of lightning arresters, although it depends on the energizing conditions, the leakage current region roughly corresponds to (2), and is the current region defined as the so-called limited voltage (10KA−
20KA) corresponds to (3) and (4). That is, an element with excellent protection characteristics has good current stability (life) in the region (2), and it is desirable that the limiting voltage related to (3) or (4) be as small as possible. From the examination of the microstructure and reaction mechanism so far, we have found that bismuth oxide (or compounds that become bismuth oxide at high temperatures, such as bismuth nitrate)
becomes a liquid phase during firing, promotes crystal growth of zinc oxide particles, dissolves ions such as chromium, and exists so as to cover the zinc oxide particles. Ions such as cobalt, nickel, manganese, chromium, and aluminum are dissolved in zinc oxide particles, but some of them also form spinel particles with antimony oxide (or those that decompose at high temperatures to form antimony oxide, such as antimony tartrate). . From this, it can be seen that the components dissolved in zinc oxide particles are mainly in the high current region (the above-mentioned
Regarding (3) and (4)), those that do not easily react with zinc oxide and exist between particles, such as bismuth oxide, are mainly in the low current region ((1) and
(2)). The spinel particles of the second phase are considered to be involved in the distribution of various ions to the zinc oxide portion and the bismuth oxide portion. Now, when preparing aqueous solutions of various salts, nitrates such as nickel, cobalt, manganese, and chromium are easily soluble in water, and antimony tartrate is also easily soluble. On the other hand, bismuth nitrate is insoluble in water and produces a white precipitate in the form of hydroxide; however, by adding concentrated nitric acid to lower the pH, the white precipitate disappears and dissolves uniformly. Bismuth ions exist stably in sufficiently concentrated nitric acid, but when this solution is reacted with a large amount of zinc oxide powder, nitric acid quickly reacts with zinc oxide according to the following formula, so Z o O + 2HNO 3 →Z o (NO 3 ) 2 +H 2 O The pH of the solution increases and bismuth ions immediately form a white precipitate. In other words, an aqueous solution of bismuth nitrate containing nitric acid appears to be a uniform aqueous solution, but when this aqueous solution is mixed with zinc oxide powder, it immediately precipitates and forms a solid phase, so it is difficult to mix with other added ionic components. They cannot be handled in the same way, and problems arise with uniform dispersibility. In particular, if these slurries are allowed to stand and dry, the aqueous solution will evaporate to dryness except for the bismuth ions, but
Bismuth is dried from the solid phase as a white precipitate, and its extremely high density makes it extremely difficult to obtain a highly uniform dry powder for bismuth, which affects the current-voltage characteristics on the low current side. It was found that it worsened the condition and had a negative effect on the life characteristics. Although the use of bismuth nitrate has been mainly discussed here, the same is true when bismuth hydrochloride is used in an alcoholic solution because it easily undergoes hydrolysis and forms the same phase if a large amount of water is present. In any case, it is difficult to mix bismuth ions with zinc oxide in a solution state, so even if this white precipitate occurs, it is necessary to dry the bismuth ion in the best possible mixed state. It has been found that by doing this, since the dispersibility of other added ions is originally good, the overall uniformity is improved and the current-voltage characteristics on the low current side are also greatly improved. As a result of various studies in consideration of mass productivity, and with the condition that drying could be performed with each element mixed as uniformly as possible, it was found that a method using a spray dryer was preferable. Furthermore, spherical granules can be obtained by adding a water-soluble binder as in the conventional method, and the granules are dried at a relatively high temperature. It was found that there are also advantages such as no need for a thermal decomposition process. This invention has been made based on the above findings, and includes a method for manufacturing a voltage nonlinear resistor containing zinc oxide as a main component.
A mixed slurry containing an aqueous metal salt solution of an additive, a precipitate of a part of an additive, and an aqueous binder is homogenized by stirring or agitation, and the mixed slurry is continuously spray-dried to remove precipitates other than the zinc oxide powder and The present invention resides in a method for producing a voltage nonlinear low antibody in which decomposition and oxidation of various salts and formation of granules are performed simultaneously. The mixed slurry is preferably prepared by adding a bismuth ion solution containing concentrated nitric acid to a slurry containing zinc oxide, an aqueous additive salt solution, and a water-soluble binder. Further, the metal salt is a compound that decomposes during spray drying, and either nitrate or tartrate can be suitably used. The temperature of the hot air during spray drying is preferably set to a temperature necessary to decompose the metal salt and a temperature that does not decompose the water-soluble binder. The present invention will be described below with reference to prototype experimental examples. Example FIG. 2 shows a schematic diagram of the mixing and granulation process in the case of a two-fluid nozzle type spray dryer as an example. In the figure, the slurry produced in the disper mill 4 is sprayed from a nozzle 11 in the spray dryer main body 6 by a slurry transport pump 6 together with compressed air from a compressor 10 (in the case of a two-fluid nozzle). The air that has passed through the heater 7 enters the main body 6 of the spray dryer (heating tower) and instantly dries the mist coming from the nozzle 11, and the dried powder is taken out from the granule outlet 12. The mixed slurry is prepared as follows. Pour about 1.5 liters of water into the disper mill and add 3% PVA.
Solution 2, surfactant 2% aqueous solution 1 and antifoaming agent
Add 20 c.c. and mix in advance. Next, predetermined amounts of nickel nitrate, cobalt nitrate, chromium nitrate, and aluminum nitrate are weighed out and dissolved in 1.0% water (first solution). Next, dissolve a predetermined amount of antimony oxide in an aqueous solution of tartaric acid to create a second liquid of 0.3 cm, and dissolve bismuth nitrate in a mixed solution of 200 c.c. of water and 100 c.c. of concentrated nitric acid to create a third liquid. Be prepared. Pour all of the first and second liquids into the disper mill and mix for about 15 minutes, then slowly mix in 10 kg of zinc oxide powder (over about 10 minutes) and mix for about 1 hour. . Finally, slowly mix in the third liquid over about 5 minutes, then mix in the third liquid for about 15 minutes.
Mix for ~1.5 hours. This mixed slurry is continuously fed to the spray dryer by a pump. The operating conditions of the spray dryer are a hot air temperature of about 250°C, an exhaust air temperature of 120°C, a spray pressure of 1.0 Kg/cm 2 , and a discharge pressure of 0.8 Kg/cm 2 . With this amount of slurry, drying is completed in about 15 minutes, and the powder is taken out from the bottom of the drying tower. The particle size distribution of the obtained powder is 150 μ or more: 40%, 100-150 μ: 40
%, 100-50μ: About 20%, almost no difference from powder mixture products. The flowability was almost the same as that of the powder mixture, and the bulk density was slightly smaller at 1.2 g/cm 3 .
When observed under a microscope, the shape was almost spherical, with some chain balls and other irregular shapes. When a part of this granulated powder is examined using a thermobalance, a weight loss is observed up to around 600°C, which is thought to be due to the decomposition of water, PVA, and surfactant, but a special No significant reaction was observed, and it is thought that the decomposition was almost complete at the time of spray drying. It was therefore found that no special pyrolysis step was required. Using the obtained powder, mold it in a regular uniaxial molder.
After pressing with a pressure of 300 kg/cm 2 and baking at 1200° C. for 4 hours, a polishing electrode was attached and the current-voltage characteristics were examined (this is referred to as sample A). Various salt solutions,
Sample B is a case in which bismuth precipitate and zinc oxide powder slurry are left to dry in batches, and then an element is made in exactly the same process as sample B, and sample C is a powder mixture. When we investigated the shrinkage rates of these A, B, and C samples, we obtained the results as shown in the table, and it is clear that the A sample and B sample shrunk better than the powder mixture C sample.
It can be seen that uniform reaction sintering is occurring. Note that the zinc oxide particle diameter was constant at approximately 15 μm for samples A, B, and C.

【表】 次に各試料の電流・電圧特性を測定した結果を
第2図に示す。図からも明らかなように、A試料
は全電流領域ですぐれた電流・電圧特性を示す
が、B試料は特に低電流領域において、C試料は
そのいずれともにおいて劣つている。 B試料では静置乾燥時のビスマスイオンの分布
不均一性が低電流領域の特性悪化をまねき、C試
料は粉末混合で最も悪い結果となつた。 噴霧乾燥方法は、すでに乾燥工程における量産
性については一般的に確認されており、ここに示
したプロトタイプのものもスケールアツプは極め
て容易である。また、ここでは二流体方式の噴霧
乾燥器について述べたが、デイスク形、その他の
方式の噴霧乾燥器についても本質的には同様であ
る。 以上のように、各種添加イオンの水溶液を使用
すること及び泥漿の乾燥方式を検討することによ
り、量産性にすぐれた製法を提供し、また、電圧
非直線抵抗体の基本特性である電流・電圧特性の
改善が実現された。
[Table] Next, the results of measuring the current/voltage characteristics of each sample are shown in Figure 2. As is clear from the figure, sample A exhibits excellent current/voltage characteristics over the entire current range, sample B particularly in the low current range, and sample C inferior in both. In sample B, non-uniform distribution of bismuth ions during static drying led to deterioration of characteristics in the low current region, and sample C had the worst results with powder mixing. The spray drying method has already been generally confirmed to be suitable for mass production in the drying process, and the prototype shown here is also extremely easy to scale up. Furthermore, although a two-fluid type spray dryer has been described here, the same is essentially true for disk-type and other types of spray dryers. As described above, by using aqueous solutions of various added ions and examining the drying method of slurry, we have provided a manufacturing method with excellent mass productivity. Improvements in properties were achieved.

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

第1図は電圧非直線抵抗体の微細構造を示す模
式図、第2図はこの発明に基く混合造粒過程を説
明する概略図、第3図はこの発明に基いて製造し
た素子及び従来法により製造した素子の電流電圧
特性を示す図である。 図中、1……酸化亜鉛を主成分とする粒子、2
……酸化ビスマスを主成分とする境界層、3……
スピネル粒子、4……デイスパーシル、5……泥
漿輸送用ポンプ、6……噴霧乾燥器本体、7……
空気加熱器、8……サイクロン、9……排風器、
10……コンプレツサ、11……ノズル、12…
…顆粒取出し口。
Fig. 1 is a schematic diagram showing the microstructure of a voltage nonlinear resistor, Fig. 2 is a schematic diagram illustrating the mixing granulation process based on this invention, and Fig. 3 is an element manufactured based on this invention and a conventional method. FIG. 3 is a diagram showing current-voltage characteristics of an element manufactured by the method. In the figure, 1...Particles whose main component is zinc oxide, 2
...Boundary layer mainly composed of bismuth oxide, 3...
Spinel particles, 4...Dispersil, 5...Sludge transport pump, 6...Spray dryer main body, 7...
Air heater, 8...cyclone, 9...exhaust fan,
10... Compressor, 11... Nozzle, 12...
...Granule outlet.

Claims (1)

【特許請求の範囲】 1 酸化亜鉛を主成分とした電圧非直線抵抗体を
製造する方法において、酸化亜鉛粉末、添加物の
金属塩水溶液、添加物の一部の沈澱物及び水溶性
バインダを含む混合泥漿を撹拌又は擾乱により均
一化し、該混合泥漿を連続的に噴霧乾燥し、前記
酸化亜鉛粉末以外の沈澱物及び各種塩の分解及び
酸化と、顆粒の形成とを同時に行なうことを特徴
とする、電圧非直線抵抗体の製造方法。 2 混合泥漿が酸化亜鉛、添加物塩水溶液、及び
水溶性バインダを含む泥漿に最終的に濃硝酸を含
むビスマスイオン溶液を加えて製造する特許請求
の範囲第1項記載の電圧非直線抵抗体の製造方
法。 3 金属塩が噴霧乾燥時に分解する化合物で硝酸
塩及び酒石酸塩のいずれかである特許請求の範囲
第1項記載の電圧非直線抵抗体の製造方法。 4 噴霧乾燥時の熱風温度を金属塩の分解に必要
な温度でかつ水溶性バインダを分解しない温度に
設定する特許請求の範囲第1項記載の電圧非直線
抵抗体の製造方法。
[Claims] 1. A method for manufacturing a voltage nonlinear resistor containing zinc oxide as a main component, comprising zinc oxide powder, an aqueous metal salt solution of an additive, a precipitate of a part of the additive, and a water-soluble binder. The mixed slurry is homogenized by stirring or agitation, and the mixed slurry is continuously spray-dried to simultaneously decompose and oxidize precipitates and various salts other than the zinc oxide powder, and form granules. , a method for manufacturing a voltage nonlinear resistor. 2. The voltage nonlinear resistor according to claim 1, wherein the mixed slurry is produced by finally adding a bismuth ion solution containing concentrated nitric acid to the slurry containing zinc oxide, an additive salt aqueous solution, and a water-soluble binder. Production method. 3. The method for manufacturing a voltage nonlinear resistor according to claim 1, wherein the metal salt is a compound that decomposes during spray drying and is either a nitrate or a tartrate. 4. The method of manufacturing a voltage nonlinear resistor according to claim 1, wherein the hot air temperature during spray drying is set to a temperature necessary for decomposing the metal salt and a temperature that does not decompose the water-soluble binder.
JP57181011A 1982-10-13 1982-10-13 Manufacturing method of voltage nonlinear resistor Granted JPS5968907A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57181011A JPS5968907A (en) 1982-10-13 1982-10-13 Manufacturing method of voltage nonlinear resistor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57181011A JPS5968907A (en) 1982-10-13 1982-10-13 Manufacturing method of voltage nonlinear resistor

Publications (2)

Publication Number Publication Date
JPS5968907A JPS5968907A (en) 1984-04-19
JPH0360163B2 true JPH0360163B2 (en) 1991-09-12

Family

ID=16093179

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57181011A Granted JPS5968907A (en) 1982-10-13 1982-10-13 Manufacturing method of voltage nonlinear resistor

Country Status (1)

Country Link
JP (1) JPS5968907A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61102003A (en) * 1984-10-25 1986-05-20 株式会社東芝 Manufacture of voltage non-linear resistor

Also Published As

Publication number Publication date
JPS5968907A (en) 1984-04-19

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