JPH0274514A - Production of high-purity silica - Google Patents

Production of high-purity silica

Info

Publication number
JPH0274514A
JPH0274514A JP22296188A JP22296188A JPH0274514A JP H0274514 A JPH0274514 A JP H0274514A JP 22296188 A JP22296188 A JP 22296188A JP 22296188 A JP22296188 A JP 22296188A JP H0274514 A JPH0274514 A JP H0274514A
Authority
JP
Japan
Prior art keywords
silica gel
acid
washing
silica
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.)
Granted
Application number
JP22296188A
Other languages
Japanese (ja)
Other versions
JPH0465007B2 (en
Inventor
Masayuki Inoue
雅之 井上
Kenji Ooka
大岡 憲司
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.)
Shin Etsu Chemical Co Ltd
Original Assignee
Shin Etsu Chemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shin Etsu Chemical Co Ltd filed Critical Shin Etsu Chemical Co Ltd
Priority to JP22296188A priority Critical patent/JPH0274514A/en
Publication of JPH0274514A publication Critical patent/JPH0274514A/en
Publication of JPH0465007B2 publication Critical patent/JPH0465007B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To economically obtain high-purity silica with hardly any impurity content, such as Na, K, Cl ions, etc., including U in a simple process using an inexpensive commercially available raw material by washing a silica gel with an acid while treating the silica gel with ultrasonic waves and then washing the resultant silica gel with water. CONSTITUTION:A commercially available gel is washed with an acid, such as sulfuric or nitric acid. In the process, the silica gel is simultaneously subjected to ultrasonic treatment and then washed with water. Ionic impurities, such as Na, K and Cl, including U in pores of the silica gel are liberated from the silica gel and the pores thereof are extended. Thereby, the impurities are extracted, passed into the outside of the silica gel system and effectively removed even by treatment at ordinary temperature. The raw material is inexpensive and readily available and the respective steps of the above-mentioned washing with the acid and water are simply operated with a few steps according to the above-mentioned method. Thereby, high-purity silica can be surely produced at a low cost.

Description

【発明の詳細な説明】 童栗上又■朋分互 本発明は、ウラン、更にはNa、に、CQイオン等の不
純物含有量が極めて少なく、電子部品封止材用充填剤な
どとして好適に用いられる高純度シリカの製造方法に関
する。
[Detailed Description of the Invention] The present invention has an extremely low content of impurities such as uranium, Na, and CQ ions, and is suitable as a filler for electronic component encapsulating materials. The present invention relates to a method for producing high-purity silica.

の   び  が  しよ゛と る 近年、シリカはLSIあるいは超LSI等の電子部品封
止材用充填剤として利用されることが多くなっているが
、この場合、シリカに含まれるウラン等が微量であって
も、これから放出されるα線がデバイスの作動誤差を引
き起こすという問題がある。このため、電子部品封止材
用充填剤として使用するシリカは高純度のものが要求さ
れ。
In recent years, silica has been increasingly used as a filler for encapsulating electronic components such as LSIs and VLSIs, but in this case, silica contains trace amounts of uranium, etc. Even if there is, there is a problem that the alpha rays emitted from this will cause operational errors in the device. For this reason, the silica used as a filler for electronic component sealants is required to be of high purity.

特にウラン含有量が0.5ppb以下であり、かつNa
、に、CQイオン等の不純物含有量がそれぞれ2 pp
m以下であることが望まれる。
In particular, the uranium content is 0.5 ppb or less, and the Na
, the content of impurities such as CQ ions is 2 pp, respectively.
It is desirable that it be less than m.

従来、高純度シリカの製造方法としては、アルカリ珪酸
塩と酸とからシリカゲルを生成させ、このシリカゲルを
酸で処理し、水洗する方法(特開昭59−54632号
、同60−42217号。
Conventionally, a method for producing high-purity silica involves producing silica gel from an alkali silicate and an acid, treating the silica gel with acid, and washing with water (JP-A-59-54632 and JP-A-60-42217).

同60−204613号、同62−3011号、同62
−83313号公報)が知られている。
No. 60-204613, No. 62-3011, No. 62
-83313) is known.

しかしながら、上記の高純度化方法では、酸処理時のシ
リカゲル形状、酸濃度、処理温度、撹拌強度等を調節し
ても、シリカ中の不純物を除去するのに限界があり、1
!子部品のソフトエラー発生を解決し得るに十分な極め
て高純度のシリカを得ることは困難であった。しかも、
上記方法は、酸処理後のび過、水洗時に多大な時間を要
する上。
However, in the above-mentioned high purification method, even if the silica gel shape, acid concentration, treatment temperature, stirring intensity, etc. during acid treatment are adjusted, there is a limit to the ability to remove impurities from the silica.
! It has been difficult to obtain silica of extremely high purity sufficient to solve the problem of soft errors in child parts. Moreover,
The above method requires a large amount of time for spreading and washing with water after acid treatment.

濾過ケーキの含水率が大きいことから乾燥、加熱処理に
要する熱エネルギー消費が莫大であるという欠点を有し
、工業的にも不都合である。
Since the water content of the filter cake is high, it has the drawback that the thermal energy required for drying and heat treatment is enormous, which is also industrially disadvantageous.

なお、高純度シリカを得る他の方法として、気相反応を
利用したもの、珪酸エステル等を加水分解して利用した
ものも知られている(特開昭59−8615号、同59
−13620号、同6〇−90811号、同60−90
812号、同6O−1809L1号、同60−1910
16号5同60−204.614号、同61−1414
4号、同61−17416号、同61−40811号、
同61−48421号、同61−270209号、同6
2−3012号、同62−12608号公報)が、これ
ら方法は、高純度シリカの′15造が高価なものとなっ
て、経済的に不利である。
In addition, as other methods for obtaining high purity silica, methods using gas phase reactions and methods using hydrolysis of silicate esters are also known (Japanese Patent Application Laid-open No. 8615/1986, 59
-13620, 60-90811, 60-90
No. 812, No. 6O-1809L1, No. 60-1910
16 No. 5 No. 60-204.614, No. 61-1414
No. 4, No. 61-17416, No. 61-40811,
No. 61-48421, No. 61-270209, No. 6
(No. 2-3012, No. 62-12608) However, these methods are economically disadvantageous because the production of high-purity silica is expensive.

従って、より高純度のシリカを工業的かつ経済的に有利
に得ることができるシリカの製造方法の開発が望まれて
いた。
Therefore, it has been desired to develop a method for producing silica that can advantageously obtain silica of higher purity industrially and economically.

本発明は、上記事情に鑑みなされたもので、ウラン、更
にはNa、に、Cαイオン等の含有量が非常に少なく、
電子部品封止材用充填剤として好適な高純度シリカを安
価な原料を用いて簡単かつ能率的に低コストで生産でき
る高純度シリカの製造方法を提供することを目的とする
The present invention was made in view of the above circumstances, and has a very low content of uranium, Na, Cα ions, etc.
An object of the present invention is to provide a method for producing high-purity silica, which can easily and efficiently produce high-purity silica suitable as a filler for electronic component sealing materials at low cost using inexpensive raw materials.

するための   び作用 本発明者は、上記目的を達成するため、鋭意検討を重ね
た結果、従来、シリカゲルは安価ではあるものの原料の
珪石に由来するウランが数1゜PPb含まれ、しかもこ
のウランの除去が困難であるとされ、上述したようにこ
のシリカゲルからウラン、その他のNa、に、Cαイオ
ン等のイオン性不純物を除去するにはかなりの手間を要
していたものであるが、シリカゲルを超音波処理しなが
ら酸洗浄することにより、ウラン、Na、に、Cαイオ
ン等を短時間で効果的に除去できることを見い出した。
In order to achieve the above object, the inventor of the present invention has conducted extensive studies and found that although silica gel is inexpensive, it contains several tens of degrees of PPb of uranium derived from the raw material silica. As mentioned above, removing ionic impurities such as uranium, other Na, and Cα ions from this silica gel requires considerable effort. It has been discovered that uranium, Na, Cα ions, etc. can be effectively removed in a short time by acid washing while treating with ultrasonic waves.

即ち、原料として市販のシリカゲルを用い、これを硫酸
、硝酸等の酸で洗浄する際、同時に超音波処理した場合
、超音波由来のキャビテーション現象で真空から数千気
圧にまで及ぶ圧力波の変動が生じ、シリカゲルの細孔中
のウラン、Na、K。
In other words, when commercially available silica gel is used as a raw material, and when it is washed with acids such as sulfuric acid or nitric acid and treated with ultrasonic waves at the same time, the cavitation phenomenon caused by the ultrasonic waves causes fluctuations in pressure waves ranging from vacuum to several thousand atmospheres. uranium, Na, and K in the pores of silica gel.

CQ等の不純物がシリカゲルから遊離し、かつシリカゲ
ル細孔が押し広げられて、これら不純物がシリカゲル系
外へ抽出移動され、かかるシリカゲルを酸処理する場合
に撹拌強度を変えたりあるいはシリカゲルを固定相とし
て酸を移動させたりしても除去に限界があった上記不純
物が、常温下の処理でも効果的に除去され、ウラン、更
にはN a 。
Impurities such as CQ are liberated from the silica gel, and the silica gel pores are expanded, and these impurities are extracted and moved out of the silica gel system. The above-mentioned impurities, which could only be removed by transferring acid, can be effectively removed even by treatment at room temperature, and uranium and even Na can be effectively removed.

K、Cαイオン等の含有量が非常に少ない高純度シリカ
が得られること、特に酸処理に続く水洗工程においても
超音波処理を行なうことにより、上記不純物がより確実
に除去されること、しかも、この方法は原料が安価で入
手容易であると共に、前記酸洗浄、水洗の各工程の操作
が簡単な上、工程も少なく、確実かつ低コストで高純度
シリカを製造し得ることを知見し1本発明をなすに至っ
たものである。
High purity silica with a very low content of K, Cα ions, etc. can be obtained, and the above impurities can be more reliably removed by ultrasonication, especially in the water washing step following the acid treatment. It was discovered that the raw materials for this method are cheap and easy to obtain, the operations of the acid washing and water washing steps are simple, the number of steps is small, and high-purity silica can be produced reliably and at low cost. This led to the invention.

以下1本発明につき更に詳述する。The present invention will be explained in more detail below.

本発明の高純度シリカの製造方法は、上述したようにシ
リカゲルを超音波処理しながら酸で洗浄した後、水洗す
るものであり、このように酸洗浄の際、同時に超音波処
理することにより、酸洗浄によってウラン、Na、に、
Cαイオン等が効果的に除去されるため、ウランが0.
5ρpb以下で。
The method for producing high-purity silica of the present invention is to wash silica gel with acid while treating it with ultrasonic waves as described above, and then washing it with water. By acid cleaning, uranium, Na,
Since Cα ions etc. are effectively removed, uranium is reduced to 0.
Less than 5ρpb.

かつNa、に、Cαイオンがそれぞれ2 ppm以下の
より高純度のシリカが製造できる。
Furthermore, it is possible to produce silica with higher purity, in which Na, Cα ions are each 2 ppm or less.

ここで、原料として使用するシリカゲルは、公知の製造
法1例えばけい酸エステルの加水分解法。
Here, the silica gel used as a raw material is produced by a known manufacturing method 1, for example, a silicate ester hydrolysis method.

イオン交換法、けい酸塩の酸による分解法など、種々の
方法によって得られたいずれのものも使用できるが、特
にアルカリけい酸塩水溶液と酸とから得られたシリカゲ
ルが有効に使用できる。また、シリカゲルの形状、粒径
、細孔径、M孔容積などに何らも制限はなく、吸着剤、
触媒担体などとして一般に市販されているもの1例えば
JIS−A型破枠状粒状シリカゲル、JIS−B型ビー
ズ状シリカゲル等の各種シリカゲルを使用することがで
きるが、特にシリカキセロゲルを使用することが好まし
く、これにより濾過などによるヒドロゲル中の水分除去
工程が省略できる。
Although any one obtained by various methods such as ion exchange method and decomposition method of silicate with acid can be used, silica gel obtained from an aqueous alkali silicate solution and an acid can be used particularly effectively. In addition, there are no restrictions on the shape, particle size, pore size, M pore volume, etc. of silica gel, and the adsorbent,
Various silica gels that are generally commercially available as catalyst carriers, such as JIS-A type broken frame-shaped granular silica gel and JIS-B type beaded silica gel, can be used, but it is particularly preferable to use silica xerogel. This makes it possible to omit the step of removing water from the hydrogel by filtration or the like.

本発明は上述したシリカゲルを原料として、超音波処理
しながら酸洗浄し、水洗して高純度シリ力を製造するも
のであるが、まず、上述したシリカゲルを酸で洗浄する
場合、酸としては塩酸、硝酸、硫酸等の鉱酸が好適に用
いられ、特に硫酸又は硝酸が好ましい。
The present invention uses the above-mentioned silica gel as a raw material, and produces high-purity silica gel by washing it with acid while treating it with ultrasonic waves and washing it with water. First, when washing the silica gel mentioned above with acid, hydrochloric acid is Mineral acids such as , nitric acid, and sulfuric acid are preferably used, with sulfuric acid and nitric acid being particularly preferred.

この場合、酸9度は必ずしも制限されないが、酸をイオ
ン交換水、蒸留水等の純水で希釈し、酸の濃度を1規定
以上として使用することが好ましい。あまり低い濃度で
はウラン等の不純物を十分除くことができない場合があ
り、1度が高くなり過ぎると水洗に使用する水を大量に
必要とし、また濃度を高くしても酸洗浄効果が比例せず
、不経済となる場合がある。
In this case, the acid concentration is not necessarily limited to 9%, but it is preferable to dilute the acid with pure water such as ion-exchanged water or distilled water and use the acid at a concentration of 1N or more. If the concentration is too low, it may not be possible to sufficiently remove impurities such as uranium, and if the 1 degree is too high, a large amount of water will be required for washing, and even if the concentration is high, the acid washing effect will not be proportional. , it may be uneconomical.

而して、本発明ではかかる酸洗浄において、超音波処理
を行なうものであるが、この場合、超音波処理の条件と
しては、特に制限はされないが例えば出力10W〜2k
W、発振周波数15〜60k Hzの超音波槽中で酸処
理することが好適である。
Therefore, in the present invention, ultrasonic treatment is performed in such acid cleaning, and in this case, the conditions for ultrasonic treatment are not particularly limited, but for example, an output of 10 W to 2 k
It is preferable to carry out the acid treatment in an ultrasonic bath with W and an oscillation frequency of 15 to 60 kHz.

また、酸洗浄は加温して行なってもよいが、本発明では
常温で酸洗浄しても不純物を十分に除去できるので、常
温で行なうことができる。
Further, although acid washing may be carried out with heating, in the present invention, impurities can be sufficiently removed even if acid washing is carried out at room temperature, so it can be carried out at room temperature.

なお、酸洗浄工程を必要により2回以上に分けて行なう
こともできる。
Note that the acid washing step can be carried out in two or more parts if necessary.

また、酸洗浄はバッチ式でも連続式でもよいが、酸洗浄
の時間は10分〜3時間とすることが好ましい。
Further, the acid cleaning may be carried out in a batch manner or in a continuous manner, but the acid cleaning time is preferably 10 minutes to 3 hours.

上述したように酸洗浄したシリカゲルは、次いでイオン
交換水、蒸留水等の純水を使用して酸を除去する水洗工
程を行なう。この場合、水洗温度は加温することができ
るが、常温でも十分である。
The silica gel that has been acid-washed as described above is then subjected to a water-washing process in which the acid is removed using pure water such as ion-exchanged water or distilled water. In this case, the washing temperature can be increased, but room temperature is sufficient.

なお、水洗する方法は通常のバッチ式、連続式を採用す
ることができる。
Note that a normal batch type or continuous type can be used for washing with water.

この水洗工程においても、上記酸洗浄と同様に超音波処
理しながら行なうことが不純物や酸をより効果的に除去
できる点から好適である。この場合の超音波処理条件も
上記順洗浄の超音波処理条件と同様とすることができる
In this water washing step as well, it is preferable to carry out ultrasonic treatment in the same manner as in the above-mentioned acid washing because impurities and acids can be removed more effectively. The ultrasonic treatment conditions in this case can also be the same as the ultrasonic treatment conditions for the above-mentioned sequential cleaning.

次に、上記のように酸洗浄し、水洗したシリカゲルは通
常のシリカゲル乾燥温度で乾燥し、必要により微粉砕し
、粒度調整するものである。
Next, the silica gel washed with acid and water as described above is dried at a normal silica gel drying temperature, and if necessary, pulverized to adjust the particle size.

1泄し房か果 以上説明したように1本発明によれば、超音波を利用し
て酸で洗浄した後、水洗するという簡単な工程によって
、半導体等の電子部品封止材用充填剤に要望されるウラ
ン、更にはNa、に、CQイオン等の含有量が極めて少
ない高純度シリカを製造することができる。更に1本発
明の製造方法は、原料として安価で入手が容易な市販シ
リカゲルを使用でき、また、酸使用量を最少限とし得る
上、特別な薬剤が不要であるので、経済性に優れており
、しかも、工程が簡単な上、原料としてキセロゲルの使
用が可能なことからが過等のヒドロゲル中の水分除去工
程を省略でき、かつ自動化して高純度シリカを連続生産
することもできるので。
As explained above, according to the present invention, a filler for encapsulating materials for electronic components such as semiconductors can be made by a simple process of washing with acid using ultrasonic waves and then washing with water. It is possible to produce high-purity silica with an extremely low content of uranium, Na, CQ ions, etc. as desired. Furthermore, the manufacturing method of the present invention can use commercially available silica gel that is inexpensive and easily available as a raw material, can minimize the amount of acid used, and does not require any special chemicals, so it is highly economical. Moreover, since the process is simple and xerogel can be used as a raw material, the step of removing excess water from the hydrogel can be omitted, and high-purity silica can be continuously produced by automation.

工業的に有利である。Industrially advantageous.

失庭態−皮較孤 以下、実施例及び比較例を示して本発明を具体的に説明
するが、本発明は下記実施例に制限されるものではない
EXAMPLES The present invention will be specifically described below with reference to examples and comparative examples, but the present invention is not limited to the following examples.

〔実施例1〕 市販シリカゲル(JIS−A型破砕品)50gと6規定
の硝酸400蔽を撹拌装置付きのフラスコに入れ、出力
100W、発振周波数27kHzの超音波槽の中で室温
下で撹拌した。2時間後。
[Example 1] 50 g of commercially available silica gel (JIS-A type crushed product) and 400 g of 6N nitric acid were placed in a flask equipped with a stirring device, and stirred at room temperature in an ultrasonic bath with an output of 100 W and an oscillation frequency of 27 kHz. . 2 hours later.

酸を廃棄し、イオン交換水を用いてp Hが6になるま
で水洗した。
The acid was discarded and washed with ion-exchanged water until the pH reached 6.

〔実施例2〕 実施例1と同様にシリカゲルを超音波槽中で酸処理し、
更にイオン交換水による水洗処理を超音波槽中で行なっ
た。
[Example 2] Similar to Example 1, silica gel was acid-treated in an ultrasonic bath,
Furthermore, washing treatment with ion-exchanged water was performed in an ultrasonic bath.

〔実施例3〕 シリカゲルとしてJIS−A型ビーズを使用すると共に
、硝酸の代わりに6規定の硫酸を使用した以外は実施例
1と同様に処理した。
[Example 3] Processing was carried out in the same manner as in Example 1 except that JIS-A type beads were used as the silica gel and 6N sulfuric acid was used instead of nitric acid.

〔実施例4〕 シリカゲルとしてJIS−B型ビーズを使用した以外は
実施例1と同様に処理した。
[Example 4] The same process as in Example 1 was carried out except that JIS-B type beads were used as the silica gel.

〔比較例1〕 酸処理工程で超音波処理を行なわない以外は実施例1と
同様に処理した。
[Comparative Example 1] Processing was carried out in the same manner as in Example 1 except that ultrasonic treatment was not performed in the acid treatment step.

〔比較例2〕 酸処理工程で超音波処理を行なわない以外は実施例3と
同様に処理した。
[Comparative Example 2] Processing was carried out in the same manner as in Example 3 except that ultrasonic treatment was not performed in the acid treatment step.

〔比較例3〕 酸処理工程で超音波処理を行なわない以外は実施例4と
同様に処理した。
[Comparative Example 3] Processing was carried out in the same manner as in Example 4 except that ultrasonic treatment was not performed in the acid treatment step.

上記実施例1〜4及び比較例1〜3で得られたシリカゲ
ルについて、不純物含有率、電気伝導率及び水洗後の含
水率を測定した。なお、比較のため、各側で使用した原
料の市販シリカゲルについても同様の測定を行なった。
The impurity content, electrical conductivity, and water content after washing were measured for the silica gels obtained in Examples 1 to 4 and Comparative Examples 1 to 3 above. For comparison, similar measurements were also performed on the commercially available silica gel used as the raw material on each side.

結果を第1表に示す。The results are shown in Table 1.

第1表の結果より、原料シリカゲルを超音波処理しなが
ら象洗浄し、水で洗浄した場合(実施例1〜4)は、超
音波処理しない場合(比較例1〜3)よりもウラン、N
a、に、CQイオン等の不純物含有量が少なく、電気伝
導度の低い高純度シリカが簡単な操作で比較的短時間で
得られることが確認された。特に、酸処理に加えて水洗
においても超音波処理した場合(実施例2)、得られた
シリカの電気伝導度が顕著に低くなり、イオン性不純物
が極めて少なくなることが認められた。
From the results in Table 1, it can be seen that when the raw material silica gel was washed with ultrasonic waves and washed with water (Examples 1 to 4), the amount of uranium and N
In a., it was confirmed that high-purity silica with a low content of impurities such as CQ ions and low electrical conductivity could be obtained in a relatively short time with simple operations. In particular, when ultrasonic treatment was applied during water washing in addition to acid treatment (Example 2), it was observed that the electrical conductivity of the obtained silica was significantly lowered and the ionic impurities were extremely reduced.

出願人  信越化学工業株式会社 代理人  弁理士 小 島 隆 同 年 続 栢1j 正 書  (自 発) 昭和63年10月190 1、事件の表示 昭和63年特許願第222961号 2、発明の名称 高純度シリカの製造方法 3、補正をする者 事件との関係 住  所 氏  名Applicant: Shin-Etsu Chemical Co., Ltd. Agent: Patent attorney Takashi Kojima Year Continued Maki 1j Positive Calligraphy (self-published) October 1988 190 1.Display of the incident 1986 Patent Application No. 222961 2. Name of the invention Manufacturing method of high purity silica 3. Person who makes corrections Relationship with the incident address full name

Claims (1)

【特許請求の範囲】[Claims] 1、シリカゲルを超音波処理しながら酸で洗浄した後、
水洗することを特徴とする高純度シリカの製造方法。
1. After washing the silica gel with acid while treating it with ultrasound,
A method for producing high-purity silica, which is characterized by washing with water.
JP22296188A 1988-09-06 1988-09-06 Production of high-purity silica Granted JPH0274514A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22296188A JPH0274514A (en) 1988-09-06 1988-09-06 Production of high-purity silica

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22296188A JPH0274514A (en) 1988-09-06 1988-09-06 Production of high-purity silica

Publications (2)

Publication Number Publication Date
JPH0274514A true JPH0274514A (en) 1990-03-14
JPH0465007B2 JPH0465007B2 (en) 1992-10-16

Family

ID=16790595

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22296188A Granted JPH0274514A (en) 1988-09-06 1988-09-06 Production of high-purity silica

Country Status (1)

Country Link
JP (1) JPH0274514A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002037620A (en) * 2000-07-25 2002-02-06 Ube Nitto Kasei Co Ltd Spherical silica particle bulk materials and method of preparing it and resin composition using it
CN101817533A (en) * 2010-04-27 2010-09-01 中国地质大学(武汉) Preparation method of electronic-level crystalline silicon powder
CN103616565A (en) * 2013-12-10 2014-03-05 连云港东海硅微粉有限责任公司 Method for detecting specific conductance of quartz material

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002037620A (en) * 2000-07-25 2002-02-06 Ube Nitto Kasei Co Ltd Spherical silica particle bulk materials and method of preparing it and resin composition using it
JP4605864B2 (en) * 2000-07-25 2011-01-05 宇部日東化成株式会社 Method for producing spherical silica particle aggregate
CN101817533A (en) * 2010-04-27 2010-09-01 中国地质大学(武汉) Preparation method of electronic-level crystalline silicon powder
CN103616565A (en) * 2013-12-10 2014-03-05 连云港东海硅微粉有限责任公司 Method for detecting specific conductance of quartz material

Also Published As

Publication number Publication date
JPH0465007B2 (en) 1992-10-16

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