JPS5848488B2 - Silica sol manufacturing method - Google Patents

Silica sol manufacturing method

Info

Publication number
JPS5848488B2
JPS5848488B2 JP53098298A JP9829878A JPS5848488B2 JP S5848488 B2 JPS5848488 B2 JP S5848488B2 JP 53098298 A JP53098298 A JP 53098298A JP 9829878 A JP9829878 A JP 9829878A JP S5848488 B2 JPS5848488 B2 JP S5848488B2
Authority
JP
Japan
Prior art keywords
solution
sodium silicate
acidic
silica sol
sludge
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
JP53098298A
Other languages
Japanese (ja)
Other versions
JPS5527822A (en
Inventor
禄生 岡
敏行 菊池
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.)
Hitachi Zosen Corp
Original Assignee
Hitachi Zosen 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 Hitachi Zosen Corp filed Critical Hitachi Zosen Corp
Priority to JP53098298A priority Critical patent/JPS5848488B2/en
Publication of JPS5527822A publication Critical patent/JPS5527822A/en
Publication of JPS5848488B2 publication Critical patent/JPS5848488B2/en
Expired legal-status Critical Current

Links

Description

【発明の詳細な説明】 本発明は、ヘドロあるいはヘドロ類似物質の凝結処理剤
として硅酸ソーダあるいは硅酸ソーダと硅酸カリウムの
混合物を酸性物質と混合して酸性硅酸ゾルを製造する方
法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing an acidic silicate sol by mixing sodium silicate or a mixture of sodium silicate and potassium silicate with an acidic substance as a coagulation treatment agent for sludge or sludge-like substances. It is something.

かかる方法において、例えば硫酸(濃度98%)の10
倍希釈液と硅酸ソーダ(J I 83号相当)の2倍希
釈液とを攪拌混合した場合、徐々にゲル化し、そして中
和域において完全にゲル化してしまう。
In such a method, for example, 10% of sulfuric acid (98% concentration)
When a 2-fold diluted solution and a 2-fold diluted solution of sodium silicate (equivalent to J I 83) are stirred and mixed, the mixture gradually gels and then completely gels in the neutralization region.

これは中性であるpH 7. 5において最短(約10
秒)にゲル化するからである。
It has a neutral pH of 7. 5, the shortest (about 10
This is because it gels in seconds).

このようにゲル化してしまうと、反応槽(混合槽)から
の除去や後使用に問題が生じる。
When gelatinized in this way, problems occur in removal from the reaction tank (mixing tank) and subsequent use.

そこで本発明は、短時間に中和域を通過させることによ
り、溶性化したゾル領域に移行させ得るシリカゾル製造
方法を提供するもので、以下その一実施例を図面に基づ
いて説明する。
Therefore, the present invention provides a method for producing silica sol that can be transferred to a solubilized sol region by passing through a neutralization region in a short period of time, and one embodiment thereof will be described below with reference to the drawings.

すなわち本発明は、反応槽1内に、シリカゾルの製造に
必要な量の酸を酸液タンク2から酸供給ポンプ3を介し
て供給し、そして酸供給ポンプ3を停止させる。
That is, in the present invention, an amount of acid necessary for producing silica sol is supplied into the reaction tank 1 from the acid liquid tank 2 via the acid supply pump 3, and then the acid supply pump 3 is stopped.

次いで攪拌装置4を作動してその攪拌羽根5を周速1
0 m / sec以上で回転させ、酸を攪拌状態にす
る。
Next, the stirring device 4 is operated to set the stirring blade 5 at a circumferential speed of 1.
Rotate at 0 m/sec or more to keep the acid in a stirring state.

この時、循環ポンプ6も運転し、反応槽1内での滞留を
防止する。
At this time, the circulation pump 6 is also operated to prevent stagnation in the reaction tank 1.

このような状態になってから硅酸ソーダ供給ポンプ7を
運転し、硅酸ソーダ溶液タンク8内の硅酸ソーダ溶液を
前記攪拌羽根5のところに、適径(lm以下)の状態で
滴下添加させる。
After reaching this state, the sodium silicate supply pump 7 is operated, and the sodium silicate solution in the sodium silicate solution tank 8 is added dropwise to the stirring blade 5 in an appropriate diameter (lm or less). let

このようにすれば、強アルカリである硅酸ソーダは0.
1秒以下で強酸側へ移行してしまう。
In this way, sodium silicate, which is a strong alkali, will be reduced to 0.
It shifts to the strong acid side in less than 1 second.

これがシリカゾル液の安定の条件である。This is the condition for stability of the silica sol liquid.

そして前述した滴下添加を続けることにより、硅酸ソー
ダ濃度の低い側から徐々に濃度の高い目的とするシリカ
ゾル液を作ることができる。
By continuing the above-mentioned dropwise addition, the desired silica sol solution can be produced, starting from the lower sodium silicate concentration and gradually increasing the concentration.

もし両液の添加順序が逆であれば、すなわち硅酸ソーダ
溶液の中に酸の溶液を添加すれば、いかに充分な攪拌を
しても、酸は拡散するどころか硅酸ソーダ溶液と反応し
てゲルを作ってしまい、沈澱してしまうことからシリカ
ヅルとして役に立たない安定物質になってしまう。
If the order of addition of both solutions is reversed, i.e., if an acid solution is added to a sodium silicate solution, no matter how thorough the stirring is, the acid will not diffuse but will react with the sodium silicate solution. It forms a gel and precipitates, resulting in a stable substance that is useless as silica crane.

したがって添加の順序を守らなければ製造はできない。Therefore, production cannot be performed unless the order of addition is followed.

すなわち、硅酸ソーダ溶液を用い酸でゲル化させるなら
ばどちらから液を添加してもよいが、ゾル液を作るには
添加順序がある。
That is, if a sodium silicate solution is used for gelation with an acid, the solution may be added in either direction, but there is an order of addition in order to make a sol solution.

さらに反応槽1において、もし攪拌不充分な状態が生じ
たらシリカゾル液は反応槽1の底部に堆積してしまうた
め、常に循環ポンプ6で循環させなければならない。
Furthermore, if insufficient stirring occurs in the reaction tank 1, the silica sol solution will accumulate at the bottom of the reaction tank 1, so it must be constantly circulated by the circulation pump 6.

このように目的とするpH=1.0〜2.0になるよう
にして循環かつ強制攪拌すれば、大量のシリカゾルを製
造することができる。
A large amount of silica sol can be produced by circulating and forcibly stirring the mixture to achieve the desired pH of 1.0 to 2.0.

このシリカゾル液は、供給ポンプ9により処理設備のタ
ンク(図示せず)へ供給される。
This silica sol liquid is supplied to a tank (not shown) of the processing equipment by a supply pump 9.

次に、循環および攪拌の意義と効果を述べる。Next, the significance and effects of circulation and stirring will be described.

A.攪拌なし又はゆるい攪拌で硅酸ソーダ中に酸性物質
を入れた場合の反応式を示せば、 Na2 0 .nSt 02 + H2 S 04
”′−”Na2S 04+ nH2 S i 03→
Na2 S 04 +H20 + ( S t 02
)。
A. The reaction formula when an acidic substance is added to sodium silicate without stirring or with gentle stirring is Na2 0 . nSt 02 + H2 S 04
"'-"Na2S 04+ nH2 Si 03→
Na2 S 04 + H20 + ( S t 02
).

となり、安定ゲル物が発生して、目的とする凝固剤とし
て使用にたえないものとなる。
As a result, a stable gel is generated, making it unsuitable for use as the intended coagulant.

B.強制攪拌により酸性物質の中へ硅酸塩を少しづつ極
加する場合の反応式を示せば、 2H2SO4+Na20’ nsi02 →H2SO4+Na2SO4+(SiO2)aq+H2
0→Na2 S 04 + H2 0 + S i (
OH )2 S 04となり、シリカゾル主成分(
S i ( OH )2 804 )を有するところの
、ヘ)の物質とは全く別な物質を製造することができる
B. The reaction formula when silicate is added little by little into an acidic substance by forced stirring is: 2H2SO4+Na20' nsi02 →H2SO4+Na2SO4+(SiO2)aq+H2
0→Na2 S 04 + H2 0 + S i (
OH)2S04, and the main component of silica sol (
S i (OH)2 804 ), which is completely different from the substance f), can be produced.

このの)によって製造した物質を汚泥やヘドロの中に攪
拌後、強アルカリ液又は硅酸ソーダと混合攪拌し中和す
ればゲル化安定物質が発生してヘドロ処理用主剤として
用いることが可能となる。
After stirring the material produced by this process into sludge or sludge, the mixture is stirred and neutralized with a strong alkaline solution or sodium silicate to generate a stable gelling substance, which can be used as the main agent for sludge treatment. Become.

上記の如くして製造した酸性硅酸ゾル(シリカゾル)を
用いてヘドロあるいはヘドロ類似物質をゲル化する場合
、ヘドロ中に酸性硅酸ゾルを添加混合後中和せしめても
、あるいはヘドロをアルカノ性とした後に酸性硅酸ゾル
を添加攪拌後中和せしめても、その添加順序に関係なく
良好な凝結固化物を得ることができる。
When gelling sludge or sludge-like substances using the acidic silicic acid sol (silica sol) produced as described above, even if the acidic silicic acid sol is added to the sludge and neutralized after mixing, or the sludge is converted into an alkanoic material. Even if the acidic silicic acid sol is added, stirred, and then neutralized, a good solidified product can be obtained regardless of the order of addition.

以上述べた本発明方法によると、反応槽内に酸性溶液を
入れて攪拌羽根により急速攪拌するとともに反応槽内の
酸性溶液を循環ポンプにより循環させて滞留を防ぐので
、硅酸ソーダあるいは硅酸ソーダと硅酸カリウムの混合
物を希釈溶解して作った溶液を前記酸性溶液に滴下添加
したときに、極めて短時間に強酸側へ移行させることが
できる。
According to the method of the present invention described above, an acidic solution is placed in a reaction tank and rapidly stirred by a stirring blade, and at the same time, the acidic solution in the reaction tank is circulated by a circulation pump to prevent stagnation. When a solution prepared by diluting and dissolving a mixture of potassium silicate and potassium silicate is added dropwise to the acidic solution, it can be shifted to the strong acid side in an extremely short time.

したがって、反応槽からの取出しが容易な酸性硅酸ゾル
を得ることができ、しかもその後のゲル化には充分な時
間を取れることから、ヘドロ処理用主剤として有利に採
用できる。
Therefore, it is possible to obtain an acidic silicic acid sol that can be easily taken out from the reaction tank, and since sufficient time is allowed for subsequent gelation, it can be advantageously employed as a main agent for sludge treatment.

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

図面は本発明の一実施例を示すフローシ一ト図である。 1・・・反応槽、2・・・酸液タンク、3・・・酸供給
タンク、4・・・攪拌装置、5・・・攪拌羽根、6・・
・循環ポンプ、7・・・硅酸ソーダ供給ポンプ、8゜゜
゛硅酸ソーダ溶液タンク、9・・・供給ポンプ。
The drawing is a flow sheet diagram showing one embodiment of the present invention. DESCRIPTION OF SYMBOLS 1... Reaction tank, 2... Acid liquid tank, 3... Acid supply tank, 4... Stirring device, 5... Stirring blade, 6...
- Circulation pump, 7... Sodium silicate supply pump, 8゜゜゛Sodium silicate solution tank, 9... Supply pump.

Claims (1)

【特許請求の範囲】[Claims] 1 ヘドロあるいはヘドロ類似物質の凝結処理剤として
硅酸ソーダあるいは硅酸ソーダと硅酸カリウムの混合物
を酸性物質と混合して酸性硅酸ゾルを製造する方法にお
いて、反応槽内に酸性溶液を入れて攪拌羽根により急速
攪拌するとともに反応槽内の酸性溶液を循環ポンプによ
り循環させて滞留を防ぎ、前記攪拌羽根のところに、硅
酸ソーダあるいは硅酸ソーダと硅酸カリウムの混合物を
希釈溶解して作った溶液を、適径の状態で滴下添加する
ことを特徴とするシリカゾル製造方法。
1. In a method of producing acidic silicic acid sol by mixing sodium silicate or a mixture of sodium silicate and potassium silicate with an acidic substance as a coagulation treatment agent for sludge or sludge-like substances, an acidic solution is placed in a reaction tank. Rapid stirring is performed using a stirring blade, and the acidic solution in the reaction tank is circulated using a circulation pump to prevent stagnation. A method for producing silica sol, characterized by adding dropwise a solution having an appropriate diameter.
JP53098298A 1978-08-11 1978-08-11 Silica sol manufacturing method Expired JPS5848488B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP53098298A JPS5848488B2 (en) 1978-08-11 1978-08-11 Silica sol manufacturing method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP53098298A JPS5848488B2 (en) 1978-08-11 1978-08-11 Silica sol manufacturing method

Publications (2)

Publication Number Publication Date
JPS5527822A JPS5527822A (en) 1980-02-28
JPS5848488B2 true JPS5848488B2 (en) 1983-10-28

Family

ID=14216003

Family Applications (1)

Application Number Title Priority Date Filing Date
JP53098298A Expired JPS5848488B2 (en) 1978-08-11 1978-08-11 Silica sol manufacturing method

Country Status (1)

Country Link
JP (1) JPS5848488B2 (en)

Also Published As

Publication number Publication date
JPS5527822A (en) 1980-02-28

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