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JPH0455967B2 - - Google Patents
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JPH0455967B2 - - Google Patents

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Publication number
JPH0455967B2
JPH0455967B2 JP16487684A JP16487684A JPH0455967B2 JP H0455967 B2 JPH0455967 B2 JP H0455967B2 JP 16487684 A JP16487684 A JP 16487684A JP 16487684 A JP16487684 A JP 16487684A JP H0455967 B2 JPH0455967 B2 JP H0455967B2
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JP
Japan
Prior art keywords
manufacturing
water
compound
silicic acid
tin
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
Application number
JP16487684A
Other languages
Japanese (ja)
Other versions
JPS6144709A (en
Inventor
Yoshiaki Koga
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.)
Tokuyama Corp
Original Assignee
Tokuyama 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
Publication date
Application filed by Tokuyama Corp filed Critical Tokuyama Corp
Priority to JP16487684A priority Critical patent/JPS6144709A/en
Publication of JPS6144709A publication Critical patent/JPS6144709A/en
Publication of JPH0455967B2 publication Critical patent/JPH0455967B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は、導電性を有する含水珪酸の製造方法
に関し、特に高温下で着色しない白色の導電性含
水珪酸を簡便に製造する方法を提供するものであ
る。 従来より含水珪酸は天然ゴム、合成ゴムの充填
剤、各種合成樹脂の不透及びブロツキング防止
剤、紙の填料、ベイント配合剤、農薬吸着担体、
粘度調節剤などとして広い分野に使用されてい
る。近年、特に上記の如きゴム、合成樹脂、塗
料、紙などに導電性を付与するために、導電性を
有する含水珪酸が要望されている。しかしなが
ら、含水珪酸は一般に電気絶縁体であり、導電性
を有していない。そそのため、例えば特開昭56−
114215〜114218号には、酸化チタンなど白色金属
酸化物粉末に酸化錫、またはアンモチモンと錫化
合物を被覆してなる白色導電性複合粉末及びその
製造方法が提案されている。すなわち、これらの
製造方法は、白色金属酸化物粉末の懸濁液に塩化
錫、または塩化アンチモンと塩化錫のアルコール
溶液を添加して処理する方法である。これに対し
て、本発明者等は、導電性を良好かつ安定して有
する含水珪酸を得るために、珪酸アルカリを酸で
中和して含水珪酸を製造するに際して、反応系に
錫化合物または錫化合物とアンチモン化合物とを
存在させる方法を提案した。(特願昭58−63756号 本発明者等は、さらに導電性を有する珪酸の製
造方法について鋭意研究を進めた結果、珪酸アル
カリを錫化合物及び水溶成弗素化合物と反応させ
ることによつて、極めて良の導電性を有し、且つ
高温において着色しない白色の含水珪酸が得られ
ることを見出し、本発明を提供するに至つた。す
なわち、本発明は珪酸アルカリと錫化合物及び水
溶性弗素化合物を含む溶液を反応させることを特
徴とする導電性を有する含水珪酸の製造方法であ
る。 本発明によれば珪酸アルカリと錫化合物及び水
溶性弗素化合物とを反応させるため生成する含水
珪酸と同時に該珪酸に弗素をドーブした酸化錫が
均一に含有されて析出する。したがつて、本発明
により得られる含水珪酸は該含水珪酸の表面およ
び内部に弗素をドーブした酸化錫が強固に含有さ
れるため、高温において着しないで且つ所望の導
電性を安定して発揮することができるものと推測
される。 本発明において珪酸アルカリと錫化合物及び水
溶性弗素化合物を反応させる方法は特に制限なく
用いられる。一般には、珪酸アルカリ水溶液を昇
温し、該水溶液中に水溶性錫化合物と水溶性弗素
化合物を含す水溶液を添加してPH調整を行行
い、珪酸アルカリ粒子を完全に析出せしめた後、
濾過水洗、乾燥、必要より粉砕し、該粉砕品を温
度500〜900℃で焼成する方法が推奨される。 本発明の珪酸アルカリとしては、例えば珪酸ナ
トリウム、珪酸カリウム、珪酸リチウム、珪酸ア
ンモニウムなどであり、これらが一般に水溶液と
して使用され、特に珪酸ナトリウム(ソーダ)の
水溶液が工業的に使用される。珪酸ナトリウム
(Na2O・SiO2)のSiO2とNa2Oのモル比(SiO2
Na2O)は1.5〜2.5が好ましく、該モル比が1.5以
下の場合はアルカリが多くなるため経済的でな
く、また、モル比が2.5以上になるとシリカへの
錫化合物の担持量が減少するため導電性の良好な
シリカが得られない。 本発明の含水珪酸に所望の導電性を付与するた
めには、前述した珪酸アルカリ水溶液にアルコー
ルを添加することが好ましい。アルコールの添加
量は珪酸アルカリ水溶液中にアルコールの容割合
が10%以下で存在させることが好ましく、10%以
上になると珪酸アルカリとアルコールのエステル
化が起こり、ゲル化物が生じるため撹拌が困難と
なる。アルコールとしては、メチルアルコール、
エチルアルコール、イソプロピルアルコール等が
好ましく用いられる。 本発明において錫化合物及び水溶性弗素化合物
は、一般に、水、アルコールなどの溶媒に溶解し
て用いることが、得られる含水珪酸に所望の導電
性を安定かつ均一に付与するために好ましい。し
たがつて、錫化合物及び水溶性弗素化合物として
は溶媒に可溶性であればよく、例えば錫化合物と
しては塩化錫が一般に用いられ、そのほか硫酸
塩、酸化物なども適宜用いられる。また、水溶性
弗素化合物としては弗化アンモニウムが好ましく
用いられる。また本発明の含水珪酸に所望の導電
性を付与するためには、珪酸アルカリ溶液におい
て、錫化合物Na2Oに対して重量比で1.6〜2.2で
存在させることが好ましい。すなわち、錫化合物
が上記1.6より少ない場合には、酸化錫の析出が
不充分であるため含水珪酸に所望の導電性を充分
に付与できず、また2.2より多くしても、導電性
の付与に一段の向上は認められない。一方、水溶
性弗素化合物は、錫化合物(重量)に対し3〜8
(重量)%の割合で存在させることが好ましい。
すなわち、水溶性弗素化合物が上記3(重量)%
より少ない場合には、酸化錫中の弗素のドーブ量
が少ないため得られる含水珪酸に、所望の導電性
を充分に付与できず、また8(重量)%より多く
しても、導電性の付与に一段の向上が認められな
い。 上記した珪酸アルカリに錫化合物及び水溶性弗
素化合物を添加して珪酸ゾルを生成する反応は、
仕込み珪酸アルカリの濃度、温度、反応終了時の
PH、撹拌などの影響が大きい。すなわち、仕込
み珪酸アルカリの濃度が高い場合にはゲル化し、
撹拌が困難となるため、一般にSiO2として2〜
10g/100mlとすることが好ましい。上記SiO2
2g/100ml以下では経済的でないばかりでなく、
珪酸ケルの生成が困難となる。温度は一般に40〜
100℃が好ましく、40℃より低い場合には反応液
の粘度が高なり、得られる含水珪酸の比表面積に
影響するため適宜調節すればよい。反応終了後の
PHは導電性に影し、PHが7以下になると導電
性は低下する。撹拌は反応が局部的に起こらない
ように、充分に効かすことが望ましい。 反応終了後の珪酸スラリー、常法により濾過水
洗して副生塩を除去した後、乾燥、粉砕、分級す
る。さらに必要により、この含水珪酸を電気炉で
500〜700℃の温度で1〜2時間焼成することによ
り、所望の導電性を有する含水珪酸を得ることが
できる。焼成方法は公知の法が特に制限なくもち
いられるが、電気炉又は瞬間的に火焔と接触させ
る方法が好ましく用いられる。 本発明は上記した含水珪酸の製造方法におい
て、珪酸アルカリと錫化合物及び水溶性弗素化合
物を反応させることによつて良な導電性を有する
微細な含水珪酸を得ることができる。かくして得
られた本発明の導電性を有る含水珪酸は、例え
ば、通電感熱紙、静電記録紙、静電塗料、帯電防
止用プラスチツクやゴム材などの充填剤として極
めて有用である。 以下、実施例を挙げるが、本発明はこれらに制
限されるものではない。なお、実施例及び比較例
における測定方法を示す。 (1) 比抵抗(Ω・cm) ブリツチ回路(横河電機製)で測定 (2) 白色度 Kett光電白度計(Kett科学研究製) 実施例 1 SiO濃度44.41%およびNa2O濃度21.65%の珪酸
ソーダ溶液540ml、水2220ml、エタノール240ml
を、容積5リツトルの内部加熱式反応器に仕込
み、液温度を60度とした。 次に水600mlに塩化錫SnCl4210gとフツ化アン
モニウム12.6gを溶解した混合液を90分で反応槽
へ添加し、添加終了後、反応温度を90℃とし、こ
の状態で20分熟成し、溶液のPHを9.10とした。
得られたスラリー溶液を濾過、水洗して得たケー
クを110℃で乾燥して含水珪酸を得た。次いで、
粉砕、分級し、電気中で650℃で60分焼成して、
比抵抗および白色度の測定に供した。その含水珪
酸についての測定値を第1表に示す。 実施例 2 実施例1において、酸ゾーダ溶液270ml、水
2484ml、エタノール246ml、塩化錫117g、フツ化
アンモニウム7.0gにしたほかは同様に製造した。
その結果を第1表に示す。 実施例 3 実施例1において、SiO2濃度44.63%及びNa2O
濃度22.24%の珪酸ソーダ溶液53ml、水2216ml、
エタノール246ml、塩化錫240g、フツ化アンモニ
ウム14.4gにしたほかは、同様に製造した。その
結果を第1表に示す。 実施例 4 実施例1において、エタノールは使用せず、水
2460mlにしたほかは、同様に製造した。その結果
を第1表に示す。 比較例 1 SiO濃度27.09%およびNa2O濃度9.24%の珪酸
ソーダ溶液1034ml、水1767mlを容積5リツトルの
内部加熱式反応器に仕込み、液温度60℃とした。 次に、水700mlに塩化錫(SnCl4)196gを溶解
し、これを90分で反応槽へ添加し、この状態で60
分保持し熟成し、溶液のPHを7.38しとた。得ら
れたスラリー溶液を濾過・水洗して得たケークを
110℃で乾燥して含水珪酸を得た。次いで粉砕・
分級し、650℃の電気炉中で60分焼成して、比抵
抗及び白色度の測定に供した。その結果を第1表
に示す。 【表】
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing conductive hydrated silicic acid, and particularly provides a method for easily producing white conductive hydrated silicic acid that does not discolor at high temperatures. Hydrous silicic acid has traditionally been used as a filler for natural rubber and synthetic rubber, as an opaque and anti-blocking agent for various synthetic resins, as a filler for paper, as a binder compound, as a pesticide adsorption carrier,
It is used in a wide range of fields, including as a viscosity modifier. In recent years, there has been a demand for hydrated silicic acid having electrical conductivity, particularly in order to impart electrical conductivity to rubber, synthetic resins, paints, paper, etc. as mentioned above. However, hydrated silicic acid is generally an electrical insulator and does not have electrical conductivity. For this reason, for example, Japanese Patent Application Laid-Open No. 1986-
Nos. 114215 to 114218 propose a white conductive composite powder obtained by coating a white metal oxide powder such as titanium oxide with tin oxide or ammothymony and a tin compound, and a method for producing the same. That is, these manufacturing methods involve adding tin chloride or an alcoholic solution of antimony chloride and tin chloride to a suspension of white metal oxide powder. On the other hand, in order to obtain hydrated silicic acid having good and stable conductivity, the present inventors added a tin compound or a tin compound to the reaction system when producing hydrated silicic acid by neutralizing alkali silicate with acid. A method was proposed in which a compound and an antimony compound were made to exist. (Japanese Patent Application No. 58-63756) As a result of further intensive research into the production method of silicic acid having electrical conductivity, the present inventors have found that by reacting an alkali silicate with a tin compound and a water-soluble fluorine compound, an extremely The present inventors have discovered that a white hydrated silicic acid having good conductivity and not discolored at high temperatures can be obtained, leading to the provision of the present invention.That is, the present invention provides a silicic acid containing an alkali silicate, a tin compound, and a water-soluble fluorine compound. This is a method for producing hydrated silicic acid having conductivity, which is characterized by reacting a solution.According to the present invention, since an alkali silicate is reacted with a tin compound and a water-soluble fluorine compound, the silicic acid is simultaneously produced with hydrated silicic acid. Fluorine-doped tin oxide is uniformly contained and precipitated. Therefore, the hydrated silicic acid obtained by the present invention contains fluorine-doped tin oxide strongly on the surface and inside of the hydrated silicic acid, so it cannot be heated at high temperatures. It is presumed that it is possible to stably exhibit the desired conductivity without causing any build-up.In the present invention, the method of reacting an alkali silicate with a tin compound and a water-soluble fluorine compound can be used without any particular restrictions.Generally, After raising the temperature of an aqueous alkali silicate solution and adjusting the pH by adding an aqueous solution containing a water-soluble tin compound and a water-soluble fluorine compound to the aqueous solution, the alkali silicate particles are completely precipitated.
The recommended method is to filter, wash with water, dry, grind if necessary, and then sinter the pulverized product at a temperature of 500 to 900°C. Examples of the alkali silicate of the present invention include sodium silicate, potassium silicate, lithium silicate, and ammonium silicate, which are generally used as an aqueous solution, and in particular, an aqueous solution of sodium silicate (soda) is used industrially. Molar ratio of SiO 2 and Na 2 O in sodium silicate (Na 2 O・SiO 2 ) (SiO 2 /
Na 2 O) is preferably 1.5 to 2.5; if the molar ratio is less than 1.5, the amount of alkali increases, making it uneconomical; if the molar ratio is more than 2.5, the amount of tin compound supported on the silica decreases. Therefore, silica with good conductivity cannot be obtained. In order to impart desired conductivity to the hydrated silicic acid of the present invention, it is preferable to add alcohol to the aqueous alkali silicate solution. The amount of alcohol added is preferably 10% or less by volume in the aqueous alkali silicate solution; if it exceeds 10%, esterification of the alkali silicate and alcohol will occur, resulting in a gelled product, making stirring difficult. . As alcohol, methyl alcohol,
Ethyl alcohol, isopropyl alcohol, etc. are preferably used. In the present invention, the tin compound and the water-soluble fluorine compound are generally preferably used after being dissolved in a solvent such as water or alcohol in order to stably and uniformly impart the desired conductivity to the resulting hydrated silicic acid. Therefore, the tin compound and the water-soluble fluorine compound need only be soluble in the solvent. For example, tin chloride is generally used as the tin compound, and sulfates, oxides, etc. may also be used as appropriate. Moreover, ammonium fluoride is preferably used as the water-soluble fluorine compound. Further, in order to impart desired conductivity to the hydrated silicic acid of the present invention, it is preferable that the tin compound is present in an alkaline silicate solution in a weight ratio of 1.6 to 2.2 relative to the tin compound Na 2 O. In other words, if the amount of the tin compound is less than 1.6 above, the precipitation of tin oxide is insufficient and the desired conductivity cannot be imparted to the hydrated silicic acid, and even if the amount is more than 2.2, the desired conductivity cannot be imparted to the hydrated silicic acid. No further improvement is permitted. On the other hand, the water-soluble fluorine compound is 3-8% of the tin compound (weight).
(by weight)%.
That is, the water-soluble fluorine compound is 3% (by weight) above.
If the amount is less than 8% (by weight), the desired conductivity cannot be imparted to the obtained hydrated silicic acid because the amount of fluorine doped in the tin oxide is small. No further improvement was observed. The reaction of adding a tin compound and a water-soluble fluorine compound to the above-mentioned alkali silicate to produce a silicate sol is as follows:
Concentration of alkali silicate charged, temperature, and at the end of the reaction
It is greatly influenced by pH, stirring, etc. In other words, if the concentration of the alkali silicate charged is high, it will gel,
Since stirring becomes difficult, SiO 2 is generally
It is preferable to set it as 10g/100ml. The above SiO 2
Less than 2g/100ml is not only uneconomical;
It becomes difficult to generate silicate kelp. Temperature is generally 40~
The temperature is preferably 100°C, and if the temperature is lower than 40°C, the viscosity of the reaction liquid increases, which affects the specific surface area of the obtained hydrous silicic acid, so it may be adjusted as appropriate. After the reaction
PH affects conductivity, and when PH becomes 7 or less, conductivity decreases. It is desirable that the stirring be sufficiently effective so that the reaction does not occur locally. After completion of the reaction, the silicic acid slurry is filtered and washed with water in a conventional manner to remove by-product salts, and then dried, pulverized, and classified. Furthermore, if necessary, this hydrated silicic acid is heated in an electric furnace.
By firing at a temperature of 500 to 700°C for 1 to 2 hours, hydrated silicic acid having desired conductivity can be obtained. As the firing method, any known method may be used without particular limitation, but an electric furnace or a method of instantaneous contact with flame is preferably used. In the method for producing hydrated silicic acid described above, the present invention makes it possible to obtain fine hydrated silicic acid having good conductivity by reacting an alkali silicate with a tin compound and a water-soluble fluorine compound. The conductive hydrated silicic acid of the present invention thus obtained is extremely useful as a filler for, for example, electrically conductive thermal paper, electrostatic recording paper, electrostatic paint, antistatic plastic, rubber material, and the like. Examples are given below, but the present invention is not limited thereto. Note that the measurement methods in Examples and Comparative Examples are shown below. (1) Specific resistance (Ω・cm) Measured with a Britsch circuit (manufactured by Yokogawa Electric) (2) Whiteness Kett photoelectric whiteness meter (manufactured by Kett Scientific Research) Example 1 SiO concentration 44.41% and Na 2 O concentration 21.65% Sodium silicate solution 540ml, water 2220ml, ethanol 240ml
was charged into an internally heated reactor with a volume of 5 liters, and the liquid temperature was set at 60 degrees. Next, a mixture of 210 g of tin chloride SnCl 4 and 12.6 g of ammonium fluoride dissolved in 600 ml of water was added to the reaction tank over 90 minutes, and after the addition was completed, the reaction temperature was raised to 90°C and aged in this state for 20 minutes. The pH of the solution was set to 9.10.
The obtained slurry solution was filtered and washed with water, and the obtained cake was dried at 110°C to obtain hydrous silicic acid. Then,
Grind, classify, and bake in electricity at 650℃ for 60 minutes.
It was used for measuring specific resistance and whiteness. Table 1 shows the measured values for the hydrated silicic acid. Example 2 In Example 1, 270 ml of acid Zoda solution, water
2484 ml, ethanol 246 ml, tin chloride 117 g, and ammonium fluoride 7.0 g, but were produced in the same manner.
The results are shown in Table 1. Example 3 In Example 1, SiO 2 concentration 44.63% and Na 2 O
53ml of sodium silicate solution with a concentration of 22.24%, 2216ml of water,
It was produced in the same manner except that 246 ml of ethanol, 240 g of tin chloride, and 14.4 g of ammonium fluoride were used. The results are shown in Table 1. Example 4 In Example 1, ethanol was not used and water was used.
It was manufactured in the same manner except that the volume was changed to 2460 ml. The results are shown in Table 1. Comparative Example 1 1034 ml of a sodium silicate solution with a SiO concentration of 27.09% and a Na 2 O concentration of 9.24% and 1767 ml of water were charged into a 5 liter internally heated reactor, and the liquid temperature was set at 60°C. Next, 196 g of tin chloride (SnCl 4 ) was dissolved in 700 ml of water, and this was added to the reaction tank over 90 minutes.
The pH of the solution was adjusted to 7.38. The cake obtained by filtering and washing the slurry solution with water is
It was dried at 110°C to obtain hydrous silicic acid. Next, crush and
It was classified and fired for 60 minutes in an electric furnace at 650°C, and then used for measurement of specific resistance and whiteness. The results are shown in Table 1. 【table】

Claims (1)

【特許請求の範囲】 1 珪酸アルカリと錫化合物及び水溶性弗素化合
物を含む溶液を反応させることを特徴とする導電
性を有する含水珪酸の製造方法。 2 珪酸アルカリが珪酸ナトリウムである特許請
求の範囲第1項記載の製造方法。 3 珪酸ナトリウムのSiO2とNa2Oのモル比
(SiO2/Na2O)が1.5〜2.5である特許請求の範囲
第2項記載の製造方法。 4 アルコールを含む珪酸アルカリ水溶液である
特許請求の範囲第1項記載の製造方法。 5 珪酸アルカリ水溶液中のアルコールの容積割
合が10%以下である特許請求の範囲第4項記載の
製造方法。 6 珪酸アルカリ溶液中に水溶性弗素化合物及び
水溶性錫化合物を含む混合溶液を添加する特許請
求の範囲第1項記載の製造方法。 7 錫化合物が塩化錫である特許請求の範囲第1
項記載の製造方法。 8 錫化合物を珪酸アルカリのアルカリに対して
重量比で1.6〜2.0添加する特許請求の範囲第1項
記載の製造方法。 9 水溶性弗素化合物が弗化アンモニウムである
特許請求の範囲第1項記載の製造方法。 10 水溶性弗素化合物を錫化合物に対して3〜
8重量%添加する特許請求の範囲第1項記載の製
造方法。 11 反応生成物を500〜900℃で焼成する特許請
求の範囲第1項記載の製造方法。
[Claims] 1. A method for producing hydrated silicic acid having electrical conductivity, which comprises reacting an alkali silicate with a solution containing a tin compound and a water-soluble fluorine compound. 2. The manufacturing method according to claim 1, wherein the alkali silicate is sodium silicate. 3. The manufacturing method according to claim 2, wherein the sodium silicate has a molar ratio of SiO 2 to Na 2 O (SiO 2 /Na 2 O) of 1.5 to 2.5. 4. The manufacturing method according to claim 1, which is an aqueous alkali silicate solution containing alcohol. 5. The manufacturing method according to claim 4, wherein the volume ratio of alcohol in the aqueous alkali silicate solution is 10% or less. 6. The manufacturing method according to claim 1, wherein a mixed solution containing a water-soluble fluorine compound and a water-soluble tin compound is added to the alkaline silicate solution. 7 Claim 1 in which the tin compound is tin chloride
Manufacturing method described in section. 8. The manufacturing method according to claim 1, wherein the tin compound is added at a weight ratio of 1.6 to 2.0 to the alkali silicate. 9. The manufacturing method according to claim 1, wherein the water-soluble fluorine compound is ammonium fluoride. 10 Water-soluble fluorine compound to tin compound
The manufacturing method according to claim 1, wherein 8% by weight is added. 11. The manufacturing method according to claim 1, wherein the reaction product is calcined at 500 to 900°C.
JP16487684A 1984-08-08 1984-08-08 Production of hydrous silicic acid having conductivity Granted JPS6144709A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16487684A JPS6144709A (en) 1984-08-08 1984-08-08 Production of hydrous silicic acid having conductivity

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16487684A JPS6144709A (en) 1984-08-08 1984-08-08 Production of hydrous silicic acid having conductivity

Publications (2)

Publication Number Publication Date
JPS6144709A JPS6144709A (en) 1986-03-04
JPH0455967B2 true JPH0455967B2 (en) 1992-09-07

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Family Applications (1)

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JP16487684A Granted JPS6144709A (en) 1984-08-08 1984-08-08 Production of hydrous silicic acid having conductivity

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Country Link
JP (1) JPS6144709A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH083479Y2 (en) * 1991-10-15 1996-01-31 積水化成品工業株式会社 Antifreeze water pipe
JP3160552B2 (en) 1997-05-21 2001-04-25 大塚化学株式会社 Tire or belt

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