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JPH049730B2 - - Google Patents
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JPH049730B2 - - Google Patents

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Publication number
JPH049730B2
JPH049730B2 JP60126897A JP12689785A JPH049730B2 JP H049730 B2 JPH049730 B2 JP H049730B2 JP 60126897 A JP60126897 A JP 60126897A JP 12689785 A JP12689785 A JP 12689785A JP H049730 B2 JPH049730 B2 JP H049730B2
Authority
JP
Japan
Prior art keywords
silica gel
hydrogen peroxide
silicic acid
hydrated silicic
acid
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
JP60126897A
Other languages
Japanese (ja)
Other versions
JPS61286212A (en
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 filed Critical
Priority to JP60126897A priority Critical patent/JPS61286212A/en
Publication of JPS61286212A publication Critical patent/JPS61286212A/en
Publication of JPH049730B2 publication Critical patent/JPH049730B2/ja
Granted legal-status Critical Current

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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E10/00Energy generation through renewable energy sources
    • Y02E10/50Photovoltaic [PV] energy

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  • Silicon Compounds (AREA)
  • Photovoltaic Devices (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は二酸化珪素原料の製造方法に関し、特
に、高純度SiO2原料の製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing a silicon dioxide raw material, and particularly to a method for producing a high purity SiO 2 raw material.

〔従来の技術〕[Conventional technology]

現在、次世代のエネルギー資源に関し太陽エネ
ルギーが注目され、太陽光発電に関する研究が進
められている。とりわけシリコン太陽電池は最も
有望視されており品質の向上および安価な製造方
法の開発が急がれている。
Currently, solar energy is attracting attention as a next-generation energy resource, and research on solar power generation is progressing. In particular, silicon solar cells are considered to be the most promising, and there is an urgent need to improve their quality and develop inexpensive manufacturing methods.

シリコン太陽電池に使うシリコンは高純度であ
ることが要求されているため、現在は半導体用に
製造されたシリコンを用いている。したがつてシ
リコン原料自体が非常に高価であり、このことが
太陽電池のコストを高くしている。
The silicon used in silicon solar cells is required to be highly pure, so silicon produced for semiconductors is currently used. Therefore, the silicon raw material itself is very expensive, which increases the cost of solar cells.

そこで太陽電池に使用出来るシリコンを高純度
の二酸化珪素を高純度の炭素を用いて汚染なく還
元して製造する試みがなされている。この方法に
よれば金属シリコンを一度トリクロルシランに換
え精製後還元を行なう半導体用シリコンの製造法
に比べエネルギー、コスト共大きく削減できる利
点を持つている。
Therefore, attempts have been made to produce silicon that can be used in solar cells by reducing high-purity silicon dioxide with high-purity carbon without contamination. This method has the advantage of greatly reducing energy and cost compared to the method of manufacturing silicon for semiconductors in which metallic silicon is first converted into trichlorosilane and then purified and then reduced.

しかし、この方法に用いられる天然の高純度の
二酸化珪素としては一部高級品として産出される
水晶があげられるだけであり、その資源量は限ら
れている。そこで豊富に存在するけい砂など純度
の悪いけい酸塩原料を精製し、太陽電池の製造に
使用可能な高純度の二酸化珪素に変える技術が望
まれている。
However, as the natural high-purity silicon dioxide used in this method, there are only some quartz crystals produced as high-quality products, and the amount of resources is limited. Therefore, there is a need for a technology to purify the abundant silica sand and other low-purity silicate raw materials and turn them into high-purity silicon dioxide that can be used in the production of solar cells.

又一般的に二酸化珪素原料の製造方法として、
アルカリ金属又はアルカリ土属金属の珪酸塩と
鉱酸の反応を水素イオン濃度1.5以下の条件で行
ない、含水珪酸を沈殿させ、該含水珪酸の沈殿物
を洗浄、乾燥、焼成する方法(例えば特開昭59−
54632)およびアルカリ珪酸塩と鉱酸とを反応
させてシリカゲルを得る方法(例えば特開昭59−
232911)等が知られている。
In addition, as a general method for producing silicon dioxide raw materials,
A method of reacting a silicate of an alkali metal or alkaline earth metal with a mineral acid under conditions of a hydrogen ion concentration of 1.5 or less to precipitate hydrated silicic acid, and washing, drying, and calcining the precipitate of hydrated silicic acid (for example, as described in JP-A No. Showa 59-
54632) and a method for obtaining silica gel by reacting an alkali silicate with a mineral acid (e.g.
232911) etc. are known.

〔発明が解決しようとする問題点〕 しかしながら上記シリカゲルおよび含水珪酸は
純度の高いSiO2からできているとはいうものの、
その純度はシリカゲルの場合通常99.5wt%程度、
高純度といわれるもので99.95wt%程度又含水珪
酸の場合99.95wt%程度の純度であり、そのまま
の状態では上記直接還元による太陽電池用シリコ
ンの製造に使用出来なかつた。
[Problems to be solved by the invention] However, although the above-mentioned silica gel and hydrated silicic acid are made of highly pure SiO2 ,
In the case of silica gel, its purity is usually around 99.5wt%.
It is said to be highly pure, and in the case of hydrated silicic acid, it has a purity of about 99.95 wt%, and it could not be used as it is for producing silicon for solar cells by the above-mentioned direct reduction.

これは通常シリカゲル又は含水珪酸中に含まれ
る不純物成分(Al、Fe、Ti、Zrなど)がシリカ
ゲル又は含水珪酸外にぬけにくいことに起因して
おり、特にTi成分が多く残留することに起因し
ていた。
This is usually due to the fact that impurity components (Al, Fe, Ti, Zr, etc.) contained in silica gel or hydrated silicic acid are difficult to escape from the silica gel or hydrated silicic acid, and in particular, it is caused by a large amount of Ti components remaining. was.

〔問題点を解決するための手段〕[Means for solving problems]

本発明は上記問題点を解決するために、アルカ
リ珪酸塩と鉱酸とを反応させてシリカゲルもしく
は含水珪酸を得た後に、その得られたシリカゲル
もしくは含水珪酸を洗浄液で洗浄する二酸化珪素
原料の製造方法において、前記反応および/また
は前記洗浄を、前記アルカリ珪酸塩中に不純物と
して含まれるTi量と当モルまたはそれ以上の過
酸化水素を含む加熱された液中でおこなうように
したものである。
In order to solve the above problems, the present invention aims to produce a silicon dioxide raw material by reacting an alkali silicate with a mineral acid to obtain silica gel or hydrated silicic acid, and then washing the obtained silica gel or hydrated silicic acid with a cleaning solution. In the method, the reaction and/or the washing are performed in a heated liquid containing hydrogen peroxide in an amount equivalent to or more than the amount of Ti contained as an impurity in the alkali silicate.

過酸化水素の具体的な加え方としてはアルカ
リ珪酸塩および/または鉱酸中に過酸化水素水を
添加混合しておく方法、アルカリ珪酸塩と鉱酸
の混合物に過酸化水素水を添加する方法、洗浄
液に過酸化水素水を用いるか又は洗浄液に過酸化
水素水を添加しておく方法等が例示される。又過
酸化水素水を添加する変わりに、過酸化水素の気
体を各液体中に吹きこんでも、金属過酸化物を酸
性溶液中に加えて反応により過酸化水素を発生さ
せてもかまわない。
Specific ways to add hydrogen peroxide include adding and mixing hydrogen peroxide to an alkali silicate and/or mineral acid, and adding hydrogen peroxide to a mixture of an alkali silicate and mineral acid. Examples include a method in which hydrogen peroxide is used as the cleaning liquid or hydrogen peroxide is added to the cleaning liquid. Moreover, instead of adding hydrogen peroxide solution, hydrogen peroxide gas may be blown into each liquid, or metal peroxide may be added to the acidic solution and hydrogen peroxide may be generated by reaction.

アルカリ珪酸塩としてはアルカリ金属およびア
ルカリ土類の珪酸塩が使用できるが、水分を含ん
だ通常水ガラスと呼ばれるアルカリ珪酸塩が好ま
れて使用される。又アルカリ珪酸塩としては経済
的にナトリウム珪酸が含まれ、又SiO2/Na2O比
が2〜3.5のものが取扱いやすいので好まれる。
As the alkali silicate, alkali metal and alkaline earth silicates can be used, but alkali silicates containing water and usually called water glass are preferably used. As the alkali silicate, sodium silicic acid is preferably included because it is economical, and those having a SiO 2 /Na 2 O ratio of 2 to 3.5 are preferred because they are easy to handle.

鉱酸としては硫酸を用いることが好まれ、又本
発明における洗浄液とはAl、Ti等の不純物が洗
浄される液体との意味であり、純水に限らず鉱酸
等の液体も含む。
It is preferable to use sulfuric acid as the mineral acid, and the term "cleaning liquid" in the present invention refers to a liquid in which impurities such as Al and Ti are washed away, and includes not only pure water but also liquids such as mineral acids.

反応時および/または洗浄時に存在させる過酸
化水素の分量は、アルカリ珪酸塩および鉱酸等の
原料に含まれる不純物量(特にチタンの量)およ
び希望とされる二酸化珪素原料純度により決めら
れるが原料中の不純物量(特にチタンの量)と等
モル以上の過酸化水素を存在させておくことが必
要である。そして反応時あるいは洗浄時に液中に
過酸化水素を存在させるときは、過酸化水素と
Ti、Alなどの金属不純物と結合力が大きい可溶
性の錯体を迅速に形成させるために反応液あるい
は洗浄液は加熱される。前記の液が加熱されるこ
とにより添加された過酸化水素のより多くが、シ
リカゲルや含水珪酸に吸着されることなく不純物
の金属と反応し、より多くの可溶性の錯体をつく
る。この錯体は水や鉱酸の洗浄液で、シリカゲル
や含水珪酸から容易に分離することができるので
高純度の二酸化珪素を得ることができる。
The amount of hydrogen peroxide to be present during the reaction and/or cleaning is determined by the amount of impurities (especially the amount of titanium) contained in the raw materials such as alkali silicates and mineral acids and the desired purity of the silicon dioxide raw material. It is necessary that hydrogen peroxide be present in an amount equal to or more than the amount of impurities (particularly the amount of titanium) in the material. When hydrogen peroxide is present in the solution during reaction or cleaning,
The reaction solution or cleaning solution is heated in order to quickly form a soluble complex with strong binding strength with metal impurities such as Ti and Al. As the liquid is heated, more of the hydrogen peroxide added reacts with impurity metals without being adsorbed by silica gel or hydrated silicic acid, creating more soluble complexes. This complex can be easily separated from silica gel and hydrated silicic acid using a washing solution of water or mineral acid, so that highly pure silicon dioxide can be obtained.

〔作用〕[Effect]

本発明によれば、シリカゲル又は含水珪酸が過
酸化水素と接触され反応させられるので、シリカ
ゲル又は含水珪酸中のチタン化合物が可溶性錯体
となつて鉱酸中あるいは洗浄液中に流出し、その
結果シリカゲル又は含水珪酸塩中のチタンの含有
量が減少する。
According to the present invention, since silica gel or hydrated silicic acid is brought into contact with hydrogen peroxide and reacted, the titanium compound in the silica gel or hydrated silicic acid becomes a soluble complex and flows out into the mineral acid or into the cleaning solution, and as a result, the silica gel or hydrated silica The content of titanium in the hydrous silicate decreases.

過酸化水素とチタンとはおよそ等モル比で可溶
性錯体を作ると考えられる。
Hydrogen peroxide and titanium are thought to form a soluble complex in approximately equimolar ratios.

また、過酸化水素を存在させているときの液を
加熱することは、不純物のTiやAlなどの金属と
過酸化水素との結合力が大きい可溶性錯体を迅速
に形成する。
In addition, heating a liquid in the presence of hydrogen peroxide quickly forms a soluble complex with a strong bond between impurities such as metals such as Ti and Al and hydrogen peroxide.

〔実施例〕〔Example〕

実施例 1 JIS3号水ガラス(水分含有量60〜63wt%、
SiO2含有量28〜30wt%)400gと純水480mlを混合
して珪酸ナトリウム水溶液とした。この溶液をか
くはんしながら25wt%の硫酸80mlをゆつくり加
えた。溶液はかくはん除中で固まりゲルとなつ
た。このゲルに対してもかくはんを続けゲルを粉
細し細かいゲルとした。得られたゲルを25wt%
硫酸800mlと30wt%の過酸化水素水30mlの混合液
に加え90℃で60分間保持した。硫酸および過酸化
水素水の混合液は上記処理により黄橙色となつて
おり、シリカゲル中のFe、Tiなどの不純物量が
混合液中に抽出されシリカゲルが洗浄されている
ことを示していた。その後該シリカゲルを濾別
し、20wt%塩酸800ml中に移し90℃で30分間保持
した。
Example 1 JIS No. 3 water glass (moisture content 60-63wt%,
SiO 2 content 28-30wt%) 400g and 480ml of pure water were mixed to prepare a sodium silicate aqueous solution. While stirring this solution, 80 ml of 25 wt% sulfuric acid was slowly added. The solution solidified into a gel during stirring. This gel was continued to be stirred to form a fine gel. 25wt% of the obtained gel
It was added to a mixture of 800 ml of sulfuric acid and 30 ml of 30 wt% hydrogen peroxide solution and held at 90°C for 60 minutes. The mixed solution of sulfuric acid and hydrogen peroxide solution turned yellow-orange due to the above treatment, indicating that impurities such as Fe and Ti in the silica gel were extracted into the mixed solution and the silica gel was washed. Thereafter, the silica gel was filtered off, transferred to 800 ml of 20 wt% hydrochloric acid, and maintained at 90°C for 30 minutes.

その後得られたシリカゲルを濾別し水洗後乾燥
した。
Thereafter, the obtained silica gel was separated by filtration, washed with water, and then dried.

得られたシリカゲルの組成を分析したところ
Al2.0ppm、Ti3.3ppm、Fe0.07ppm未満、
Zr1.3ppmの値であつた。
Analysis of the composition of the silica gel obtained
Al2.0ppm, Ti3.3ppm, Fe less than 0.07ppm,
The Zr value was 1.3ppm.

比較例 1 硫酸に過酸化水素水を加えなかつた以外は実施
例1と同様の操作を行ないシリカゲルを得た。得
られたシリカゲルを実施例1同様分析したところ
Al2.0ppm、Ti13ppm、Fe0.08ppm未満、
Zr1.4ppmの値であつた。
Comparative Example 1 Silica gel was obtained by carrying out the same operation as in Example 1 except that hydrogen peroxide solution was not added to the sulfuric acid. The obtained silica gel was analyzed in the same manner as in Example 1.
Al2.0ppm, Ti13ppm, Fe less than 0.08ppm,
The Zr value was 1.4ppm.

上記実施例とくらべるとTiの値が高く実施例
においてTiが除去されていることがわかる。
When compared with the above examples, the Ti value is higher, and it can be seen that Ti has been removed in the examples.

実施例 2 上記JIS3号水ガラス100gを直径0.794mmの穴を
有するノズルから25wt%硫酸200mlと30wt%過酸
化水素水5mlの混合液中にゆつくりと注入した。
注入された3号水ガラスは鉱酸中で直径約1mmの
ヒモ状の白色含水珪酸となつた。
Example 2 100 g of the above JIS No. 3 water glass was slowly poured into a mixed solution of 200 ml of 25 wt% sulfuric acid and 5 ml of 30 wt% hydrogen peroxide through a nozzle having a hole with a diameter of 0.794 mm.
The injected No. 3 water glass became string-like white hydrated silicic acid with a diameter of about 1 mm in the mineral acid.

その後この混合液および含水珪酸を90℃に加熱
し30分間保つた。その後含水珪酸を濾別し、水洗
後乾燥した。
Thereafter, this mixed solution and hydrated silicic acid were heated to 90°C and maintained for 30 minutes. Thereafter, the hydrated silicic acid was filtered off, washed with water, and then dried.

得られた含水珪酸の組成を分析したところ、
Al30ppm、Ti1.4ppm、Fe2.6ppm、Zr2.6ppmで
あつた。
Analysis of the composition of the obtained hydrated silicic acid revealed that
The contents were 30ppm Al, 1.4ppm Ti, 2.6ppm Fe, and 2.6ppm Zr.

比較例 2 過酸化水素水を硫酸に混合しなかつた以外は実
施例2と同様の操作を行ない含水珪酸を得た。得
られた含水珪酸の組成を実施例2と同様分析した
ところAl45ppm、Ti25ppm、Fe3.1ppm、
Zr4.6ppmであつた。
Comparative Example 2 Hydrous silicic acid was obtained by carrying out the same operation as in Example 2, except that hydrogen peroxide solution was not mixed with sulfuric acid. The composition of the obtained hydrated silicic acid was analyzed in the same manner as in Example 2, and it was found that Al45ppm, Ti25ppm, Fe3.1ppm,
Zr was 4.6ppm.

上記実施例とくらべるとAlおよびTiの値が高
く実施例においてAlおよびTiが除去されている
ことがわかる。
When compared with the above examples, the values of Al and Ti are higher, and it can be seen that Al and Ti are removed in the examples.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、得られる二酸化珪素原料中に
不純物量として含まれるTiの含有量を従来の
1/10以下にまで簡単な操作により減少させるこ
とができ、これにより容易に純度の高い二酸化珪
素原料を得ることができる。
According to the present invention, the content of Ti contained as an impurity in the obtained silicon dioxide raw material can be reduced to 1/10 or less of the conventional amount by a simple operation, thereby easily producing highly pure silicon dioxide. raw materials can be obtained.

Claims (1)

【特許請求の範囲】[Claims] 1 アルカリ珪酸塩と鉱酸とを反応させてシリカ
ゲルもしくは含水珪酸を得た後に、その得られた
シリカゲルもしくは含水珪酸を洗浄液で洗浄する
二酸化珪素原料の製造方法において、前記反応お
よび/または前記洗浄を、前記アルカリ珪酸塩中
に不純物として含まれるTi量と当モルまたはそ
れ以上の過酸化水素を含む加熱された液中でおこ
なうことを特徴とする二酸化珪素原料の製造方
法。
1. A method for producing a silicon dioxide raw material in which silica gel or hydrated silicic acid is obtained by reacting an alkali silicate and a mineral acid, and then the obtained silica gel or hydrated silicic acid is washed with a cleaning liquid, in which the reaction and/or the washing is performed. A method for producing a silicon dioxide raw material, characterized in that the process is carried out in a heated liquid containing hydrogen peroxide in an amount equal to or more than the mole of Ti contained as an impurity in the alkali silicate.
JP60126897A 1985-06-11 1985-06-11 Production of sio2 raw material Granted JPS61286212A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60126897A JPS61286212A (en) 1985-06-11 1985-06-11 Production of sio2 raw material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60126897A JPS61286212A (en) 1985-06-11 1985-06-11 Production of sio2 raw material

Publications (2)

Publication Number Publication Date
JPS61286212A JPS61286212A (en) 1986-12-16
JPH049730B2 true JPH049730B2 (en) 1992-02-21

Family

ID=14946581

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60126897A Granted JPS61286212A (en) 1985-06-11 1985-06-11 Production of sio2 raw material

Country Status (1)

Country Link
JP (1) JPS61286212A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101450346B1 (en) 2006-03-15 2014-10-14 알이에스씨 인베스트먼츠 엘엘씨 Method for making silicon for solar cells and other applications
JP4842395B1 (en) * 2010-11-02 2011-12-21 株式会社Reiメディカル Monolith porous body manufacturing method

Also Published As

Publication number Publication date
JPS61286212A (en) 1986-12-16

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