JPH0555179B2 - - Google Patents
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- Publication number
- JPH0555179B2 JPH0555179B2 JP59240136A JP24013684A JPH0555179B2 JP H0555179 B2 JPH0555179 B2 JP H0555179B2 JP 59240136 A JP59240136 A JP 59240136A JP 24013684 A JP24013684 A JP 24013684A JP H0555179 B2 JPH0555179 B2 JP H0555179B2
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- JP
- Japan
- Prior art keywords
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- weight percent
- dispersion
- parts
- 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.)
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Links
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 51
- 239000006185 dispersion Substances 0.000 claims description 47
- 239000000377 silicon dioxide Substances 0.000 claims description 24
- 239000003381 stabilizer Substances 0.000 claims description 21
- 239000000843 powder Substances 0.000 claims description 18
- 238000009826 distribution Methods 0.000 claims description 15
- 239000010419 fine particle Substances 0.000 claims description 14
- 229920001577 copolymer Polymers 0.000 claims description 11
- 150000003839 salts Chemical class 0.000 claims description 10
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 claims description 5
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 4
- WSFSSNUMVMOOMR-UHFFFAOYSA-N formaldehyde Natural products O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims description 4
- KVBGVZZKJNLNJU-UHFFFAOYSA-N naphthalene-2-sulfonic acid Chemical compound C1=CC=CC2=CC(S(=O)(=O)O)=CC=C21 KVBGVZZKJNLNJU-UHFFFAOYSA-N 0.000 claims description 4
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 4
- 229920003145 methacrylic acid copolymer Polymers 0.000 claims description 3
- 230000000694 effects Effects 0.000 description 15
- 239000013049 sediment Substances 0.000 description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 12
- DGVVWUTYPXICAM-UHFFFAOYSA-N β‐Mercaptoethanol Chemical compound OCCS DGVVWUTYPXICAM-UHFFFAOYSA-N 0.000 description 11
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 description 10
- 238000002474 experimental method Methods 0.000 description 8
- 238000006116 polymerization reaction Methods 0.000 description 7
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 6
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 6
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 239000003505 polymerization initiator Substances 0.000 description 6
- 239000007864 aqueous solution Substances 0.000 description 5
- 239000002270 dispersing agent Substances 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- ROOXNKNUYICQNP-UHFFFAOYSA-N ammonium peroxydisulfate Substances [NH4+].[NH4+].[O-]S(=O)(=O)OOS([O-])(=O)=O ROOXNKNUYICQNP-UHFFFAOYSA-N 0.000 description 4
- VAZSKTXWXKYQJF-UHFFFAOYSA-N ammonium persulfate Chemical compound [NH4+].[NH4+].[O-]S(=O)OOS([O-])=O VAZSKTXWXKYQJF-UHFFFAOYSA-N 0.000 description 4
- 229910001870 ammonium persulfate Inorganic materials 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000000178 monomer Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000002002 slurry Substances 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- 229910000519 Ferrosilicon Inorganic materials 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 239000004568 cement Substances 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 238000005227 gel permeation chromatography Methods 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000012299 nitrogen atmosphere Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 238000010992 reflux Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229920002126 Acrylic acid copolymer Polymers 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 239000004342 Benzoyl peroxide Substances 0.000 description 1
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 1
- 201000010001 Silicosis Diseases 0.000 description 1
- 229920002125 Sokalan® Polymers 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 235000019400 benzoyl peroxide Nutrition 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000004649 carbonic acid derivatives Chemical class 0.000 description 1
- 239000012986 chain transfer agent Substances 0.000 description 1
- 150000003841 chloride salts Chemical class 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethyl mercaptane Natural products CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- -1 isopropyl alcohol Chemical class 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 239000004584 polyacrylic acid Substances 0.000 description 1
- 239000011164 primary particle Substances 0.000 description 1
- 239000012925 reference material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000011163 secondary particle Substances 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Landscapes
- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
〔産業上の利用分野〕
本発明は微粒子シリカ粉末の水系分散安定剤に
関する。更に詳しくは、分散性が良好で且つ長時
間保存しても沈降物やハードケーキを生成せず、
再分散性の良い微粒子シリカ粉末の水系分散安定
剤に関する。
〔従来の技術及び問題点〕
微粒子シリカとはフエロシリコンやシリコンメ
タルの製造時に発生するガスを集塵することによ
り得られる産業副産物で、その用途はコンクリー
ト混和剤やプラスチツクのフイラー、農薬のバイ
ンダー等である。しかし微粒子シリカは一般に平
均粒径が0.1μm程度でありその取扱いは必ずしも
容易ではない。特に粉じんの飛散による環境汚染
や珪肺は大きな問題であり、用途開発の妨げとな
つている。この問題を解決するために、微粒子シ
リカ粉末をスラリー化(特開昭59−111963)する
方法が知られている。しかしこの方法では長期安
定性や再分散性が悪く、更に沈降物がハードケー
キを生成するという欠点を有している。
〔問題点を解決するための手段〕
本発明は上記した従来の技術の欠点を改善すべ
くなされたもので、微粒子シリカの分散性が良好
で且つ長時間保存しても沈降物やハードケーキを
生成せず、再分散性の良い微粒子シリカ粉末の水
系分散安定剤を提供するものである。本発明で言
う微粒子シリカとは、シリコンメタルやフエロシ
リコン等の製造時に副生されるもので、シリカを
70%以上含有し比表面積が10万〜30万cm2/gのも
のである。
一般に微粉末の懸濁液(スラリー)の製造には
分散剤と呼ばれる界面活性剤が使用されており、
その分散作用により微粉末は水中に安定に懸濁し
た分散系となる。しかし、この分散系も本来熱力
学的に不安定なので長時間放置すると微粉末粒子
は沈降する。一般に分散性が良好なほど沈降した
粒子は細密充填に近い沈降物になるので、硬く再
分散しにくい沈澱物、即ちハードケーキをつく
る。従つて、分散系を作つたのち直ぐ分散系を使
用する場合には分散剤は非常に優れた効果を有し
ているが、長時間保存して使用する場合はハード
ケーキが生成されるので再分散性が悪いという問
題が生じる。従来の微粒子シリカ用の分散剤は微
粉末の二次粒子を一次粒子にほぐす作用と、ほぐ
れた粒子が再び凝集するのを防ぐ作用が強いが、
沈降後にハードケーキを生成しやすく長時間保存
する場合には十分満足なものとはいえず改善が望
まれていた。
本発明者らは、微粒子シリカに対する分散効果
を有し且つ沈降物がハードケーキを生成しない作
用を有する分散安定剤を見い出すべく鋭意研究し
た結果、上記の両作用を有する分散安定剤を見い
出し本発明を完成した。
即ち本発明は(メタ)アクリル酸と(メタ)ア
クリル酸エステルのコポリマー又はその塩からな
るか、又はこれにβ−ナフタリンスルホン酸ホル
マリン縮合物及びポリビニルアルコールから選ば
れる1種又は2種以上を併用してなる微粒子シリ
カ粉末の水系分散安定剤を提供するものである。
本発明に使用される(メタ)アクリル酸と(メ
タ)アクリル酸エステルのコポリマー又はその塩
の合成は、一般に重合開始剤を用い前記単量体成
分を共重合させる。重合は溶媒中で行なう。この
際使用される溶媒は、水、イソプロピルアルコー
ル等の低級アルコール、トルエン等の炭化水素等
が用いられる。
水系重合の場合に用いられる代表的な重合開始
剤はアンモニウム又はアルカリ金属の過硫酸塩あ
るいは過酸化水素等の水溶性重合開始剤である。
水以外を溶媒する重合には、ベンゾイルパーオ
キシド等のパーオキサイドやアゾビスイソブチロ
ニトリル等のアゾ化合物等が重合開始剤として用
いられる。
分子量分布のコントロールは、重合開始剤量、
重合温度、溶媒濃度及び連鎖移動剤量等の組合せ
により行なう。重合温度は溶媒の種類や重合開始
剤量等により適宜定められるが、一般に0〜150
℃の範囲である。
このように得られた共重合物はそのままでも微
粒子シリカの分散安定剤として使用できるが、必
要に応じて更にアルカリ性物質で中和して用いる
ことも可能である。
アルカリ性物質としては一価金属及び二価金属
の水酸化物、塩化物及び炭酸塩、アンモニア、有
機アミン等が挙げられる。
本発明によれば、特定の分子量分布を有する上
記共重合物(塩)が、優れた効果をもたらすこと
が見出された。本発明に於て、化合物の分子量分
布とは、ポリアクリル酸を基準物質とするゲルパ
ーミツシヨンクロマトグラフイーにより求められ
るものであり、分子量500未満が30重量パーセン
ト以下、分子量500〜10000未満が10〜90重量パー
セント、分子量10000〜25000未満が10〜90重量パ
ーセント、分子量25000以上が30重量パーセント
以下のものであることが必要である。上記分子量
分布より低分子量が多くなると、微粒子シリカ粉
末の分散効果は優れるがハードケーキ生成防止効
果がうすれ、又上記分子量分布より高分子量が多
くなると粉末に対する凝集効果が顕著となり分散
効果が小さくなり期待する効果が得にくい。
本発明による分散安定剤の使用量は、微粒子シ
リカ粉末に対し0.01〜2重量パーセントが望まし
い。
本発明の分散安定剤は上記共重合物(塩)単独
で用いてもよいが、他の分散剤であるβ−ナフタ
リンスルホン酸ホルマリン縮合物、或は安定剤で
あるポリビニルアルコールから選ばれる1種又は
2種以上を併用することにより、より優れた効果
を示す。
本発明の分散安定剤の使用に際して、アトライ
ター、サンドミル、ロールミル、ボールミル、ホ
モジナイザー、ミキサーなどのいずれの分散機器
を用いてもよい。
〔発明の効果〕
本発明によれば、微粒子シリカの分散性が良好
で且つ長時間保存しても沈降物やハードケーキを
生成せず、再分散性の良い水系分散安定剤が提供
され、この水系分散安定剤を用いることにより、
微粒子シリカ粉末のスラリー化が可能となり、そ
の取扱がきわめて容易となる。その結果得られる
微粒子シリカのスラリーはコンクリート混和材、
肥料のコーテイング材、セメント添加材、石膏添
加材、耐火レンガ用添加材等への用途に用いられ
て優れた効果を発揮し得る。
〔実施例〕
以下実施例により本発明を詳述するが、本発明
はこれらに限定されるものではない。
実施例 1
微粒子シリカ粉末としてmicropoz(ノルウエ
ー、ノルセムセメント社製のシリカヒユーム、比
重2.10、比表面積20000m2/Kg、シリカ分91%)
を用いた。分散安定剤を含む水溶液500ml中に微
粒子シリカ1000gを加えスパーテルで撹拌した
後、ホモジナイザー(特殊機器工業(株)製)で10分
間混合して分散液を得た。この分散液の粘度をB
型粘度計で測定した後50mlの乳化試験管に入れ、
20℃の恒温室に静置し30日後及び90日後の分散安
定性を評価した。
この30日、90日後の分散安定性の評価は沈降物
の有無及び沈降物の硬さと再分散性の容易さを定
性的に判定した。
沈降物の有無
○;沈降物なし
△;僅かに沈降している
×;50%以上沈降している
沈降物の硬さと再分散性
○;上澄液を撹拌すると分散する
△;柔かくスパーテルで容易に崩れ再分散する
×;硬く再分散しない
実験に用いたアクリル酸とアクリル酸メチルの
コポリマー()は下記方法により合成した。
温度計、撹拌機、滴下ロート、ガス導入管及び
還流冷却器を備えたガラス製反応容器に、水200
部を仕込み撹拌下に反応容器内を窒素置換し、窒
素雰囲気下で沸点まで加熱した。次いでアクリル
酸160部、アクリル酸メチル40部からなる混合物
と、過硫酸アンモニウム4部、水32部の水溶液及
び2メルカプトエタノール8部、水40部の水溶液
を90分で添加し(75℃)、更に1部の過硫酸アン
モニウムを水8部に溶解させたものを90分で添加
した。添加完結後、過酸化水素50部を加え120分
間沸点に温度を保持して重合を完了させた。その
後カセイソーダ水溶液にて中和を行ない(中和度
0.85対アクリル酸)共重合体水溶液を得た。
得られた共重合体塩()の分子量分布は次表
の如くであつた。
[Industrial Field of Application] The present invention relates to an aqueous dispersion stabilizer for fine-particle silica powder. More specifically, it has good dispersibility and does not produce sediment or hard cake even when stored for a long time.
This invention relates to an aqueous dispersion stabilizer for fine silica powder with good redispersibility. [Prior art and problems] Particulate silica is an industrial byproduct obtained by collecting dust from gases generated during the production of ferrosilicon and silicon metal, and its uses include concrete admixtures, plastic fillers, and pesticide binders. etc. However, fine particle silica generally has an average particle size of about 0.1 μm, and handling thereof is not necessarily easy. In particular, environmental pollution and silicosis due to the scattering of dust are serious problems and are hindering the development of applications. In order to solve this problem, a method is known in which fine-particle silica powder is made into a slurry (Japanese Patent Laid-Open No. 111963/1983). However, this method has the disadvantage that long-term stability and redispersibility are poor, and furthermore, the sediment forms a hard cake. [Means for Solving the Problems] The present invention has been made to improve the above-mentioned drawbacks of the conventional technology, and it has good dispersibility of fine silica particles and does not produce sediment or hard cake even after long storage. The present invention provides an aqueous dispersion stabilizer for fine-particle silica powder that does not form and has good redispersibility. The fine particle silica referred to in the present invention is a by-product during the production of silicon metal, ferrosilicon, etc.
It contains 70% or more and has a specific surface area of 100,000 to 300,000 cm 2 /g. Generally, a surfactant called a dispersant is used to produce a suspension (slurry) of fine powder.
Due to its dispersion action, the fine powder becomes a dispersion system in which it is stably suspended in water. However, this dispersion system is inherently thermodynamically unstable, and if left for a long time, the fine powder particles will settle. In general, the better the dispersibility, the more closely packed the sedimented particles are, resulting in a hard cake that is harder to redisperse. Therefore, if the dispersion system is used immediately after making it, the dispersant has a very good effect, but if it is stored for a long time and used, a hard cake will be generated and it should not be reused. A problem arises in that the dispersibility is poor. Conventional dispersants for fine-particle silica have a strong effect of loosening the secondary particles of fine powder into primary particles and preventing the loosened particles from agglomerating again.
It tends to form a hard cake after sedimentation and is not fully satisfactory when stored for a long time, so improvements have been desired. The present inventors conducted extensive research to find a dispersion stabilizer that has a dispersion effect on fine-particle silica and prevents the precipitation from forming a hard cake. As a result, the present inventors discovered a dispersion stabilizer that has both of the above-mentioned effects, and the present invention has been made. completed. That is, the present invention consists of a copolymer of (meth)acrylic acid and (meth)acrylic acid ester or a salt thereof, or a combination thereof with one or more selected from β-naphthalene sulfonic acid formalin condensate and polyvinyl alcohol. The present invention provides an aqueous dispersion stabilizer for fine-particle silica powder. The copolymer of (meth)acrylic acid and (meth)acrylic acid ester used in the present invention or a salt thereof is generally synthesized by copolymerizing the monomer components using a polymerization initiator. Polymerization is carried out in a solvent. The solvent used at this time includes water, lower alcohols such as isopropyl alcohol, and hydrocarbons such as toluene. Typical polymerization initiators used in water-based polymerizations are water-soluble polymerization initiators such as ammonium or alkali metal persulfates or hydrogen peroxide. For polymerization using a solvent other than water, peroxides such as benzoyl peroxide and azo compounds such as azobisisobutyronitrile are used as polymerization initiators. Molecular weight distribution can be controlled by controlling the amount of polymerization initiator,
This is carried out by combining the polymerization temperature, solvent concentration, amount of chain transfer agent, etc. The polymerization temperature is determined appropriately depending on the type of solvent, amount of polymerization initiator, etc., but is generally 0 to 150°C.
℃ range. The copolymer thus obtained can be used as it is as a dispersion stabilizer for fine particle silica, but if necessary, it can be further neutralized with an alkaline substance before use. Examples of alkaline substances include hydroxides, chlorides, and carbonates of monovalent metals and divalent metals, ammonia, organic amines, and the like. According to the present invention, it has been found that the above copolymer (salt) having a specific molecular weight distribution provides excellent effects. In the present invention, the molecular weight distribution of a compound is determined by gel permeation chromatography using polyacrylic acid as a reference material. It is necessary that the molecular weight is 10 to 90% by weight, the molecular weight of 10,000 to less than 25,000 is 10 to 90% by weight, and the molecular weight of 25,000 or more is 30% by weight or less. If the molecular weight is lower than the above molecular weight distribution, the dispersion effect of fine silica powder will be excellent, but the effect of preventing hard cake formation will be weakened.If the molecular weight is higher than the molecular weight distribution above, the agglomeration effect on the powder will be noticeable and the dispersion effect will be reduced. It is difficult to obtain the desired effect. The amount of the dispersion stabilizer used according to the present invention is preferably 0.01 to 2 percent by weight based on the particulate silica powder. The dispersion stabilizer of the present invention may be used alone as the above-mentioned copolymer (salt), but one type selected from β-naphthalene sulfonic acid formalin condensate as another dispersant, or polyvinyl alcohol as a stabilizer Or, a combination of two or more types exhibits more excellent effects. When using the dispersion stabilizer of the present invention, any dispersion equipment such as an attritor, sand mill, roll mill, ball mill, homogenizer, mixer, etc. may be used. [Effects of the Invention] According to the present invention, there is provided an aqueous dispersion stabilizer in which fine particle silica has good dispersibility, does not produce sediment or hard cake even when stored for a long time, and has good redispersibility. By using an aqueous dispersion stabilizer,
It becomes possible to form fine-particle silica powder into a slurry, and its handling becomes extremely easy. The resulting slurry of particulate silica is used as a concrete admixture.
It can be used for applications such as fertilizer coating materials, cement additives, gypsum additives, firebrick additives, etc., and exhibits excellent effects. [Examples] The present invention will be explained in detail below with reference to Examples, but the present invention is not limited thereto. Example 1 Micropoz (silica hume manufactured by Norsem Cement, Norway, specific gravity 2.10, specific surface area 20000 m 2 /Kg, silica content 91%) was used as fine silica powder.
was used. 1000 g of fine silica particles were added to 500 ml of an aqueous solution containing a dispersion stabilizer, stirred with a spatula, and then mixed for 10 minutes with a homogenizer (manufactured by Tokushu Kiki Kogyo Co., Ltd.) to obtain a dispersion. The viscosity of this dispersion is B
After measuring with a type viscometer, put it into a 50ml emulsification test tube,
The dispersion stability was evaluated after 30 days and 90 days after being left in a constant temperature room at 20°C. The dispersion stability was evaluated after 30 and 90 days by qualitatively determining the presence or absence of sediment, the hardness of the sediment, and the ease of redispersibility. Presence or absence of sediment ○: No sediment △: Slight sedimentation ×: Hardness and redispersibility of sediment that has settled by 50% or more ○: Disperses when the supernatant is stirred △: Soft and easy to use with a spatula The copolymer () of acrylic acid and methyl acrylate used in the experiment was synthesized by the following method. In a glass reaction vessel equipped with a thermometer, stirrer, dropping funnel, gas inlet tube and reflux condenser, add 200 ml of water.
The inside of the reaction vessel was purged with nitrogen while stirring, and heated to the boiling point under a nitrogen atmosphere. Next, a mixture consisting of 160 parts of acrylic acid and 40 parts of methyl acrylate, an aqueous solution of 4 parts of ammonium persulfate and 32 parts of water, and an aqueous solution of 8 parts of 2-mercaptoethanol and 40 parts of water were added over 90 minutes (at 75°C), and then A solution of 1 part ammonium persulfate in 8 parts water was added over 90 minutes. After the addition was complete, 50 parts of hydrogen peroxide was added and the temperature was maintained at the boiling point for 120 minutes to complete the polymerization. After that, neutralize with aqueous caustic soda solution (neutralization degree
0.85 to acrylic acid) copolymer aqueous solution was obtained. The molecular weight distribution of the obtained copolymer salt (2) was as shown in the following table.
【表】
分散安定剤の添加量は微粒子シリカに対し0.25
重量パーセント(固形分として)添加した。尚静
置期間中の分散液のPHを6.0〜7.0の範囲となるよ
うに酸でコントロールした。評価結果を表−1に
示す。[Table] The amount of dispersion stabilizer added is 0.25 per particulate silica.
Weight percent (as solids) was added. The pH of the dispersion liquid during the standing period was controlled with acid to be in the range of 6.0 to 7.0. The evaluation results are shown in Table-1.
【表】【table】
【表】
表−1の結果より、実験No.1の無添加分散液
は、粘度が7340ポイズときわめて高く、又沈降物
が生じ分散安定性が乏しい。
分散剤β−ナフタリンスルホン酸ホルマリン縮
合物を添加した実験No.2では分散液の粘度低減効
果は見られるが、沈降物が生じ安定性が乏しい。
安定剤であるポリビニルアルコールを添加した
実験No.3は、沈降物が生じにくく安定性の向上は
認められるが分散液の粘度が上昇し実用性に欠け
る。
これらの比較例に比し、本発明に係わる分散安
定剤を添加した実験No.4〜No.7では、分散液の粘
度低減及び分散安定効果が顕著であり、低粘度で
しかも90日間静置後も沈降物が生じないきわめて
優れた分散安定性を示した。
実施例 2
実施例1と同様に微粒子シリカ粉末の分散液を
製造しその分散安定性を評価した。
分散安定剤として分子量分布の異なる下記サン
プルを合成した。
●サンプルL
温度計、撹拌機、滴下ロート、ガス導入管及
び還流冷却器を備えたガラス製反応容器に水
200部を仕込み、撹拌下に反応容器内を窒素置
換し窒素雰囲気下で75℃まで加熱した。次いで
アクリル酸200部と過硫酸アンモニウム4部、
水50部の水溶液及びメルカプトエタノール8
部、水50部の水溶液を90分で添加(75℃)し、
更に1部の過硫酸アンモニウムを水10部に溶解
させたものを90分で添加した。
添加完結後、過酸化水素50部を加え120分間
沸点に温度を保持し重合を完了させた。その
後、カセイソーダ水溶液にて中和を行ない(α
=0.7)重合体水溶液を得た。
このサンプルの分子量分布をゲルパーミツシ
ヨンクロマトグラフイーにより求めた。
分子量500未満;3重量パーセント
〃 500〜10000未満;64重量パーセント
〃 10000〜25000未満;31重量パーセント
〃 25000以上;2重量パーセント
●サンプルM
サンプルLと同様に行ない重合物を得た。但
し2−メルカプトエタノールを20部とした。こ
のサンプルの分子量分布は下記の通りであり、
分子量10000〜25000の部分が少ないサンプルで
ある。
分子量500未満;9重量パーセント
〃 500〜10000未満;84重量パーセント
〃 10000〜25000未満;6重量パーセント
〃 25000以上;1重量パーセント
●サンプルN
サンプルLと同様に行ない重合物を得た。但
し2−メルカプトエタノールを3部とした。こ
のサンプルの分子量分布は下記の通りであり、
分子量25000以上が多いサンプルである。
分子量500未満;1重量パーセント
〃 500〜10000未満;17重量パーセント
〃 10000〜25000未満;47重量パーセント
〃 25000以上;35重量パーセント
●サンプルO
サンプルLと同様に行ない、共重合物を得
た。但しモノマーをアクリル酸140部、アクリ
ル酸メチル60部とした。このサンプルの分子量
分布は下記の通りであつた。
分子量500未満;5重量パーセント
〃 500〜10000未満;62重量パーセント
〃 10000〜25000未満;32重量パーセント
分子量25000以上;1重量パーセント
●サンプルLと同様に行ない、共重合物を得た。
但しモノマーをアクリル酸140部、アクリル酸
メチル60部とした。又2−メルカプトエタノー
ルを20部とした。このサンプルの分子量分布は
下記の通りであり、分子量10000〜25000の部分
が少ないサンプルである。
分子量500未満;10重量パーセント
〃 500〜10000未満;85重量パーセント
〃 10000〜25000未満;4重量パーセント
〃 25000以上;1重量パーセント
●サンプルQ
サンプルLと同様に行ない共重合物を得た。
但しモノマーをアクリル酸140部、アクリル酸
メチル60部とした。又2−メルカプトエタノー
ルを3部とした。このサンプルの分子量分布は
下記の通りであり分子量25000以上が多いサン
プルである。
分子量500未満;1重量パーセント
〃 500〜10000未満;15重量パーセント
〃 10000〜25000未満;46重量パーセント
〃 25000以上;38重量パーセント
分散安定剤の添加量は微粒子シリカ粉末に対し
0.25重量パーセント(固形分)とした。評価結果
を表−2に示す。[Table] From the results in Table 1, the additive-free dispersion of Experiment No. 1 had an extremely high viscosity of 7340 poise, and also produced sediment and poor dispersion stability. In Experiment No. 2 in which the dispersant β-naphthalene sulfonic acid formalin condensate was added, an effect of reducing the viscosity of the dispersion liquid was observed, but sediment was formed and stability was poor. In Experiment No. 3, in which polyvinyl alcohol as a stabilizer was added, precipitation was less likely to occur and stability was improved, but the viscosity of the dispersion increased and was impractical. Compared to these comparative examples, in experiments No. 4 to No. 7 in which the dispersion stabilizer according to the present invention was added, the effect of reducing the viscosity of the dispersion and stabilizing the dispersion was remarkable, and the viscosity was low and the dispersion stabilized for 90 days. The dispersion showed excellent dispersion stability with no precipitation. Example 2 A dispersion of fine silica powder was produced in the same manner as in Example 1, and its dispersion stability was evaluated. The following samples with different molecular weight distributions were synthesized as dispersion stabilizers. ●Sample L Water was poured into a glass reaction vessel equipped with a thermometer, stirrer, dropping funnel, gas inlet tube, and reflux condenser.
After charging 200 parts, the inside of the reaction vessel was purged with nitrogen while stirring and heated to 75°C under a nitrogen atmosphere. Next, 200 parts of acrylic acid and 4 parts of ammonium persulfate,
Aqueous solution of 50 parts water and 8 parts mercaptoethanol
50 parts of water was added over 90 minutes (75°C),
Additionally, 1 part of ammonium persulfate dissolved in 10 parts of water was added over 90 minutes. After the addition was completed, 50 parts of hydrogen peroxide was added and the temperature was maintained at the boiling point for 120 minutes to complete the polymerization. After that, neutralize with aqueous caustic soda solution (α
=0.7) An aqueous polymer solution was obtained. The molecular weight distribution of this sample was determined by gel permeation chromatography. Molecular weight less than 500; 3 weight percent; 500 to less than 10,000; 64 weight percent; 10,000 to less than 25,000; 31 weight percent; 25,000 or more; 2 weight percent. However, the amount of 2-mercaptoethanol was 20 parts. The molecular weight distribution of this sample is as follows,
This sample has a small amount of molecular weight 10,000 to 25,000. Molecular weight less than 500; 9 weight percent; 500 to less than 10,000; 84 weight percent; 10,000 to less than 25,000; 6 weight percent; 25,000 or more; 1 weight percent ●Sample N A polymer was obtained in the same manner as Sample L. However, the amount of 2-mercaptoethanol was 3 parts. The molecular weight distribution of this sample is as follows,
This is a sample with many molecules having a molecular weight of 25,000 or more. Molecular weight less than 500; 1 weight percent 〃 500 to less than 10,000; 17 weight percent 〃 10,000 to less than 25,000; 47 weight percent 〃 25,000 or more; 35 weight percent ●Sample O A copolymer was obtained in the same manner as Sample L. However, the monomers were 140 parts of acrylic acid and 60 parts of methyl acrylate. The molecular weight distribution of this sample was as follows. Molecular weight less than 500; 5 weight percent 〃 500 to less than 10,000; 62 weight percent 〃 10,000 to less than 25,000; 32 weight percent Molecular weight 25,000 or more; 1 weight percent ● The same procedure as Sample L was carried out to obtain a copolymer.
However, the monomers were 140 parts of acrylic acid and 60 parts of methyl acrylate. Also, 2-mercaptoethanol was made into 20 parts. The molecular weight distribution of this sample is as shown below, and the sample has a small portion with a molecular weight of 10,000 to 25,000. Molecular weight less than 500; 10 weight percent; 500 to less than 10,000; 85 weight percent; 10,000 to less than 25,000; 4 weight percent; 25,000 or more; 1 weight percent ●Sample Q A copolymer was obtained in the same manner as Sample L.
However, the monomers were 140 parts of acrylic acid and 60 parts of methyl acrylate. In addition, 2-mercaptoethanol was added to 3 parts. The molecular weight distribution of this sample is as shown below, and most of the samples have a molecular weight of 25,000 or more. Molecular weight less than 500; 1 weight percent 〃 500 to less than 10,000; 15 weight percent 〃 10,000 to less than 25,000; 46 weight percent 〃 25,000 or more; 38 weight percent The amount of dispersion stabilizer added is based on the fine particle silica powder.
0.25 weight percent (solid content). The evaluation results are shown in Table-2.
【表】
表−2の結果より、サンプルL及びOを用いた
実験No.1及びNo.4の分散液は、粘度が低く又90日
間静置後においても沈降物を生ぜず、きわめて優
れた分散安定性を示した。
一方、分子量10000〜25000の部分が少ないサン
プルM及びPを用いた実験No.2及びNo.5の分散液
は、粘度低減結果は認められるが沈降物が生じ安
定性が乏しい。
更に分子量25000以上が多いサンプルN及びQ
を用いた実験No.3及びNo.6の分散液は、安定性は
認められるが粘度がきわめて高い。[Table] From the results in Table 2, the dispersions of Experiments No. 1 and No. 4 using Samples L and O had low viscosity and did not produce sediment even after standing for 90 days, and were extremely excellent. It showed dispersion stability. On the other hand, the dispersions of Experiments No. 2 and No. 5 using Samples M and P with a small amount of molecular weights from 10,000 to 25,000 showed a reduction in viscosity, but produced sediment and had poor stability. Samples N and Q with more molecular weights of 25,000 or more
The dispersion liquids of Experiments No. 3 and No. 6, which were used, were stable but had extremely high viscosity.
Claims (1)
ステルのコポリマー又はその塩からなり、該コポ
リマー又はその塩が次の分子量分布を有するもの
である微粒子シリカ粉末の水系分散安定剤。 分子量500未満;30重量パーセント以下 分子量500〜10000未満;10〜90重量パーセント 分子量10000〜25000未満;10〜90重量パーセン
ト 分子量25000以上;30重量パーセント以下 2 (メタ)アクリル酸と(メタ)アクリル酸エ
ステルのコポリマー又はその塩と、β−ナフタリ
ンスルホン酸ホルマリン縮合物及びポリビニルア
ルコールから選ばれる1種又は2種以上とからな
り、該コポリマー又はその塩が次の分子量分布を
有するものである微粒子シリカ粉末の水系分散安
定剤。 分子量500未満;30重量パーセント以下 分子量500〜10000未満;10〜90重量パーセント 分子量10000〜25000未満;10〜90重量パーセン
ト 分子量25000以上;30重量パーセント以下[Claims] 1. An aqueous dispersion stabilizer for fine-particle silica powder consisting of a copolymer of (meth)acrylic acid and (meth)acrylic acid ester or a salt thereof, wherein the copolymer or salt thereof has the following molecular weight distribution: . Molecular weight less than 500; 30 weight percent or less Molecular weight 500 to less than 10,000; 10 to 90 weight percent Molecular weight 10,000 to less than 25,000; 10 to 90 weight percent Molecular weight 25,000 or more; 30 weight percent or less2 (meth)acrylic acid and (meth)acrylic acid Fine particle silica powder consisting of an ester copolymer or a salt thereof, and one or more selected from β-naphthalene sulfonic acid formalin condensate and polyvinyl alcohol, and the copolymer or salt thereof has the following molecular weight distribution: Aqueous dispersion stabilizer. Molecular weight less than 500; 30 weight percent or less Molecular weight 500 to less than 10,000; 10 to 90 weight percent Molecular weight 10,000 to less than 25,000; 10 to 90 weight percent Molecular weight 25,000 or more; 30 weight percent or less
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59240136A JPS61118130A (en) | 1984-11-14 | 1984-11-14 | Aqueous dispersion stabilizer of fine-particle silica powder |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59240136A JPS61118130A (en) | 1984-11-14 | 1984-11-14 | Aqueous dispersion stabilizer of fine-particle silica powder |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61118130A JPS61118130A (en) | 1986-06-05 |
JPH0555179B2 true JPH0555179B2 (en) | 1993-08-16 |
Family
ID=17055033
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59240136A Granted JPS61118130A (en) | 1984-11-14 | 1984-11-14 | Aqueous dispersion stabilizer of fine-particle silica powder |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61118130A (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH064845B2 (en) * | 1987-06-24 | 1994-01-19 | 第一工業製薬株式会社 | Dispersant for stable liquid drilling method |
DE10225123A1 (en) * | 2002-06-06 | 2003-12-18 | Goldschmidt Ag Th | Highly concentrated aqueous dispersion containing hydrophilic microfine metal oxide particles and dispersing agents |
KR20070043142A (en) * | 2005-10-20 | 2007-04-25 | 삼성전기주식회사 | Thiol dispersant and sulfide phosphor paste composition comprising the same |
GB0526231D0 (en) | 2005-12-22 | 2006-02-01 | Eastman Kodak Co | Dispersant for reducing viscosity of solids |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4854150A (en) * | 1971-11-09 | 1973-07-30 | ||
JPS51131554A (en) * | 1975-05-12 | 1976-11-16 | Toyo Ink Mfg Co Ltd | Aqueous pispersion of resin curable at lower temperatures |
JPS5554358A (en) * | 1978-10-18 | 1980-04-21 | Shinetsu Unit Kk | Coating composition |
JPS5618661A (en) * | 1979-07-24 | 1981-02-21 | Chuo Hatsumei Kenkyusho:Kk | Lye inhibitor for water paint |
JPS5753474A (en) * | 1980-07-24 | 1982-03-30 | Lonza Ag | Manufacture of 2-(2-aminothiazole-4-yl)-2- (syn)-methoxyiminoacetic acid ester |
JPS5792031A (en) * | 1980-11-28 | 1982-06-08 | Denki Kagaku Kogyo Kk | Liquid for surface-treatment of polyvinyl alcohol film |
JPS57119945A (en) * | 1981-01-19 | 1982-07-26 | Dainippon Ink & Chem Inc | Aqueous composition |
JPS5925858A (en) * | 1982-08-03 | 1984-02-09 | Shikoku Kaken Kogyo Co Ltd | Adhesive composition and lightweight decorative laminate using the same |
-
1984
- 1984-11-14 JP JP59240136A patent/JPS61118130A/en active Granted
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4854150A (en) * | 1971-11-09 | 1973-07-30 | ||
JPS51131554A (en) * | 1975-05-12 | 1976-11-16 | Toyo Ink Mfg Co Ltd | Aqueous pispersion of resin curable at lower temperatures |
JPS5554358A (en) * | 1978-10-18 | 1980-04-21 | Shinetsu Unit Kk | Coating composition |
JPS5618661A (en) * | 1979-07-24 | 1981-02-21 | Chuo Hatsumei Kenkyusho:Kk | Lye inhibitor for water paint |
JPS5753474A (en) * | 1980-07-24 | 1982-03-30 | Lonza Ag | Manufacture of 2-(2-aminothiazole-4-yl)-2- (syn)-methoxyiminoacetic acid ester |
JPS5792031A (en) * | 1980-11-28 | 1982-06-08 | Denki Kagaku Kogyo Kk | Liquid for surface-treatment of polyvinyl alcohol film |
JPS57119945A (en) * | 1981-01-19 | 1982-07-26 | Dainippon Ink & Chem Inc | Aqueous composition |
JPS5925858A (en) * | 1982-08-03 | 1984-02-09 | Shikoku Kaken Kogyo Co Ltd | Adhesive composition and lightweight decorative laminate using the same |
Also Published As
Publication number | Publication date |
---|---|
JPS61118130A (en) | 1986-06-05 |
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