JPH0812399A - Admixture composition for concrete product - Google Patents

Admixture composition for concrete product

Info

Publication number
JPH0812399A
JPH0812399A JP15483994A JP15483994A JPH0812399A JP H0812399 A JPH0812399 A JP H0812399A JP 15483994 A JP15483994 A JP 15483994A JP 15483994 A JP15483994 A JP 15483994A JP H0812399 A JPH0812399 A JP H0812399A
Authority
JP
Japan
Prior art keywords
mol
concrete
admixture composition
copolymer
monomer
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
JP15483994A
Other languages
Japanese (ja)
Other versions
JP3290304B2 (en
Inventor
Fujio Yamato
富士桜 倭
Masaro Shimoda
政朗 下田
Kazue Kitagawa
和重 北川
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.)
Kao Corp
Original Assignee
Kao 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 Kao Corp filed Critical Kao Corp
Priority to JP15483994A priority Critical patent/JP3290304B2/en
Publication of JPH0812399A publication Critical patent/JPH0812399A/en
Application granted granted Critical
Publication of JP3290304B2 publication Critical patent/JP3290304B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B24/00Use of organic materials as active ingredients for mortars, concrete or artificial stone, e.g. plasticisers
    • C04B24/16Sulfur-containing compounds
    • C04B24/161Macromolecular compounds comprising sulfonate or sulfate groups
    • C04B24/163Macromolecular compounds comprising sulfonate or sulfate groups obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B24/00Use of organic materials as active ingredients for mortars, concrete or artificial stone, e.g. plasticisers
    • C04B24/24Macromolecular compounds
    • C04B24/26Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • C04B24/2641Polyacrylates; Polymethacrylates
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2103/00Function or property of ingredients for mortars, concrete or artificial stone
    • C04B2103/50Defoamers, air detrainers

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Curing Cements, Concrete, And Artificial Stone (AREA)

Abstract

PURPOSE:To lower concrete viscosity, to decrease surface bubbles and to improve compaction by allowing an admixture composition to consist of a copolymer obtained by polymerizing a specific monomer and a monomer selected between two kinds of compounds and a defoaming agent. CONSTITUTION:A copolymer A having the weight-average molecular weight of 3000-1000000 is obtained by polymerizing the monomer (a) expressed by formula I and one or more kinds of the monomers selected from the compounds expressed by formulas II and III in the mol ratio of (a)/(b)=0.1/100-100/100. The copolymer A and the defoaming agent B such as dimethyl polysiloxane are blended in the ratio (weight ratio of solid matter) of A/B=100/0.01-5.0. In the formula I, each of R1 and R2 is hydrogen or methyl, m1 is 0-2, AO is a 2-3C oxyalkylene, (n) is 110-300, X is H or a 1-3C alkyl. In the formulas II and III, each of R3-R5 is H, methyl or (CH2)m2COOM2, R6 is H or methyl, each of M1, M2 and Y is H, an alkali metal, alkaline earth metal, ammonium, an alkylammonium or a substituted alkyl ammonium and m2 is 0-2.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明はコンクリート製品用混和
剤組成物に関する。更に詳しくは、コンクリート二次製
品の製造時に使用するコンクリート混和剤として用いら
れ、振動締め固め製品や高流動充填コンクリート製品の
表面に発生する気泡の低減および遠心力による締め固め
製品の製造において、コンクリートの締め固め性を向上
させ、成型時間の短縮を可能とする混和剤組成物に関す
るものである。
FIELD OF THE INVENTION The present invention relates to an admixture composition for concrete products. More specifically, it is used as a concrete admixture used in the production of secondary concrete products, and in the production of compacted products by the reduction of bubbles generated on the surface of vibration compacted products and high-fluidity filled concrete products and centrifugal force, The present invention relates to an admixture composition capable of improving compaction property and shortening molding time.

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】従来、
コンクリート製品には、コンクリートの型枠内に注入し
た後に、内部又は外部振動機で締め固めを行う振動製品
とパイル、ポール、ヒューム管のように遠心力による締
め固めを行う遠心製品がある。
2. Description of the Related Art Conventionally, the problems to be solved by the invention
Concrete products include a vibrating product that is compacted by an internal or external vibrator after being poured into a concrete formwork, and a centrifugal product that is compacted by centrifugal force, such as piles, poles, and fume tubes.

【0003】これらの製品に使用されるコンクリートは
強度を確保するために、高性能減水剤、例えば、ナフタ
レン系 (ナフタレンスルホン酸ホルムアルデヒド縮合物
)、メラミン系 (メラミンスルホン酸ホルムアルデヒド
縮合物 )等の混和剤が必須となっている。
The concrete used in these products has a high performance water reducing agent such as a naphthalene type (naphthalene sulfonic acid formaldehyde condensate) in order to secure strength.
), Melamine-based (melamine sulfonic acid formaldehyde condensate) and other admixtures are essential.

【0004】しかし、高性能減水剤を添加したコンクリ
ートは一定の流動性 (スランプ値)の発現は可能である
が、コンクリートの粘性が高まり、締め固め性が低下す
る傾向にある。
However, although concrete having a high-performance water-reducing agent can exhibit a certain fluidity (slump value), the viscosity of the concrete increases and the compaction tends to decrease.

【0005】従って、振動製品においてはコンクリート
に含まれる気泡と充填時に巻き込んだ気泡が脱泡できず
に残り、硬化したコンクリートの表面の美観は著しく悪
いものになっている。また、遠心製品は締め固めに要す
る時間が長く必要となり、生産性が低下する。
Therefore, in the vibrating product, the air bubbles contained in the concrete and the air bubbles entrained at the time of filling cannot be defoamed and remain, and the appearance of the surface of the hardened concrete is remarkably poor. Further, the centrifugal product requires a long time for compaction, which lowers productivity.

【0006】これらのことから、混和剤組成物として、
減水剤を損なうことなく、コンクリート粘性を低下させ
る混和剤が望まれている。
From these things, as an admixture composition,
Admixtures that reduce the viscosity of concrete without damaging the water reducing agent are desired.

【0007】[0007]

【課題を解決するための手段】本発明者らは、鋭意研究
の結果、保水性能の大きいアルキレンオキシドを有する
分散剤の骨格がコンクリートの粘性の低下に有効であ
り、しかもアルキレンオキシドの 110〜300 モルの範囲
の高付加モル数において極めて有効であることを見出し
た。更に、消泡剤を加えた分散剤組成物とすることで、
コンクリート材料間の摩擦低減や気泡連行の抑制によ
り、表面気泡の低減と締め固めの向上が可能となるもの
である。
As a result of earnest research, the inventors of the present invention have found that a skeleton of a dispersant having an alkylene oxide having a high water-retaining property is effective in reducing the viscosity of concrete, and the alkylene oxide has a viscosity of 110 to 300. It has been found to be extremely effective at high added mole numbers in the molar range. Furthermore, by using a dispersant composition containing an antifoaming agent,
By reducing friction between concrete materials and suppressing entrainment of bubbles, it is possible to reduce surface bubbles and improve compaction.

【0008】即ち、本発明は、下記の一般式(A) で表さ
れる単量体(a) と下記の一般式(B)及び(C) で表される
化合物の中から選ばれる1種以上の単量体(b) とを重合
して得られる共重合体 (イ) および消泡剤 (ロ) を必須
成分とするコンクリート製品用混和剤組成物に関する。
That is, the present invention is one selected from a monomer (a) represented by the following general formula (A) and a compound represented by the following general formulas (B) and (C). The present invention relates to an admixture composition for concrete products, which comprises a copolymer (a) obtained by polymerizing the above monomer (b) and an antifoaming agent (b) as essential components.

【0009】[0009]

【化3】 Embedded image

【0010】(式中、R1, R2:水素、メチル基 m1 :0〜2の整数 AO :炭素数2〜3のオキシアルキレン基 n : 110〜300 の整数 X :水素または炭素数1〜3のアルキル基 を表す。)(Wherein R 1 and R 2 are hydrogen and a methyl group m 1 is an integer of 0 to 2 AO is an oxyalkylene group having a carbon number of 2 to 3 n is an integer of 110 to 300 X is hydrogen or a carbon number of 1 ~ Represents an alkyl group of 3).

【0011】[0011]

【化4】 [Chemical 4]

【0012】(式中、R3〜R5 :水素、メチル基、(C
H2)m2COOM2 R6 :水素、メチル基 M1,M2,Y :水素、アルカリ金属、アルカリ土類金属、ア
ンモニウム、アルキルアンモニウムまたは置換アルキル
アンモニウム m2 :0〜2の整数 を表す。)本発明に使用する共重合体 (イ) と類似構造
の不飽和結合を有するポリアルキレングリコールモノエ
ステル系単量体とアクリル酸系及び/又は不飽和ジカル
ボン酸系単量体との共重合物類としては、公知特許 (特
公昭59-18338、特公平2-78978 、特公平2-7898、特公平
2-7901、特公平2-11542 、特開平3-75252 、特開昭59-1
62163)がある。しかし、これらアルキレン鎖を持つポリ
カルボン酸塩をコンクリート製品用混和剤組成物として
用いても、コンクリートの粘性の低下が充分ではなく、
しかも気泡連行性が大きく、締め固め性の向上や表面気
泡の低減には至らない。
(In the formula, R 3 to R 5 : hydrogen, methyl group, (C
H 2 ) m 2 COOM 2 R 6 : hydrogen, methyl group M 1 , M 2 , Y: hydrogen, alkali metal, alkaline earth metal, ammonium, alkylammonium or substituted alkylammonium m 2 : represents an integer of 0 to 2 . ) Copolymer used in the present invention (a) Copolymer of a polyalkylene glycol monoester monomer having an unsaturated bond having a similar structure to an acrylic acid-based and / or unsaturated dicarboxylic acid-based monomer Known classes of patents (Japanese Patent Publication No. 59-18338, Japanese Patent Publication No. 2-78978, Japanese Patent Publication No. 2-7898, Japanese Patent Publication No.
2-7901, JP-B2-11542, JP-A-3-75252, JP-A-59-1
62163). However, even when using a polycarboxylic acid salt having these alkylene chains as an admixture composition for concrete products, the decrease in the viscosity of concrete is not sufficient,
Moreover, since the air bubble entrainment is large, the compaction property cannot be improved and the surface air bubbles cannot be reduced.

【0013】本発明者等はオキシアルキレン基の鎖長に
ついて種々検討した結果、ある特定領域の高鎖長 (付加
モル数= 110〜300)範囲において、減粘性が極めて高
く、消泡剤と併用することで減粘性と気泡連行性をさら
に改善するものである。即ち、公知特許 (前述の共重合
物に関する特許) のようなエチレンオキシド及び/又は
プロピレンオキシドのモル数が2〜100 モルの範囲では
充分な効果が発現されない。
As a result of various studies on the chain length of the oxyalkylene group, the present inventors found that the viscosity was extremely high in the high chain length (additional mole number = 110 to 300) range of a certain specific region, and it was used together with an antifoaming agent. By doing so, the viscosity reduction and bubble entrainment are further improved. That is, when the number of moles of ethylene oxide and / or propylene oxide is within the range of 2 to 100 moles as in the known patents (the patents relating to the above-mentioned copolymers), a sufficient effect is not exhibited.

【0014】本発明の共重合体において、一般式(A) で
表される単量体(a) としては、メトキシポリエチレング
リコール、メトキシポリエチレンポリプロピレングリコ
ール、エトキシポリエチレングリコール、エトキシポリ
エチレンポリプロピレングリコール、プロポキシポリエ
チレングリコール、プロポキシポリエチレンポリプロピ
レングリコール等の片末端アルキル封鎖ポリアルキレン
グリコールとアクリル酸、メタクリル酸又は脂肪酸の脱
水素 (酸化) 反応物とのエステル化物やアクリル酸、メ
タクリル酸又は脂肪酸の脱水素 (酸化) 反応物へのエチ
レンオキシド、プロピレンオキシド付加物が用いられ
る。ポリアルキレングリコールの付加モル数は 110〜30
0 であり、エチレンオキシド、プロピレンオキシドの両
付加物についてはランダム付加、ブロック付加、交互付
加等のいずれでも用いることができる。ポリアルキレン
グリコールの付加モル数が 110未満の場合は分離抵抗性
に劣り、 300を超えると流動性が低下する。
In the copolymer of the present invention, examples of the monomer (a) represented by the general formula (A) include methoxy polyethylene glycol, methoxy polyethylene polypropylene glycol, ethoxy polyethylene glycol, ethoxy polyethylene polypropylene glycol and propoxy polyethylene glycol. , An esterification product of a polyalkylene glycol with one terminal alkyl-blocked such as propoxy polyethylene polypropylene glycol and a dehydrogenation (oxidation) reaction product of acrylic acid, methacrylic acid or a fatty acid, or a dehydrogenation (oxidation) reaction product of acrylic acid, methacrylic acid or a fatty acid And ethylene oxide and propylene oxide adducts thereof are used. The number of added moles of polyalkylene glycol is 110-30
It is 0, and both additions of ethylene oxide and propylene oxide can be used in any of random addition, block addition, alternating addition, and the like. When the number of added moles of polyalkylene glycol is less than 110, the separation resistance is poor, and when it exceeds 300, the fluidity is lowered.

【0015】また、一般式(B) で表される化合物として
は、アクリル酸、メタクリル酸、クロトン酸及びこれら
の金属塩が挙げられる。また、不飽和ジカルボン酸系単
量体として、無水マレイン酸、マレイン酸、無水イタコ
ン酸、イタコン酸、無水シトラコン酸、シトラコン酸、
フマル酸、又はこれのアルカリ金属塩、アルカリ土類金
属塩、アンモニウム塩、アミン塩、置換アミン塩が使用
される。
Examples of the compound represented by the general formula (B) include acrylic acid, methacrylic acid, crotonic acid and their metal salts. Further, as the unsaturated dicarboxylic acid-based monomer, maleic anhydride, maleic acid, itaconic anhydride, itaconic acid, citraconic anhydride, citraconic acid,
Fumaric acid or an alkali metal salt, alkaline earth metal salt, ammonium salt, amine salt or substituted amine salt thereof is used.

【0016】また、一般式(C) で表される化合物として
は、アリルスルホン酸、メタリルスルホン酸、又はこれ
らのアルカリ金属塩、アルカリ土類金属塩、アンモニウ
ム塩、アミン塩、置換アミン塩が使用される。
Examples of the compound represented by the general formula (C) include allylsulfonic acid, methallylsulfonic acid, or their alkali metal salts, alkaline earth metal salts, ammonium salts, amine salts and substituted amine salts. used.

【0017】本発明の共重合体を構成する単量体(a) と
単量体(b) の反応単位は、単量体(a) /単量体(b) =
0.1/100 〜 100/100(モル比) の範囲が特に、流動性
と分離抵抗性に優れる。上記のモル比が 0.1/100 より
も小さい場合は流動性が低下傾向になり、 100/100 よ
りも大きい場合は分離抵抗性が低下傾向となる。
The reaction units of the monomer (a) and the monomer (b) constituting the copolymer of the present invention are monomer (a) / monomer (b) =
The range of 0.1 / 100 to 100/100 (molar ratio) is particularly excellent in fluidity and separation resistance. When the above molar ratio is less than 0.1 / 100, the fluidity tends to decrease, and when it exceeds 100/100, the separation resistance tends to decrease.

【0018】本発明の共重合体 (イ) の製造法は公知の
方法で製造することができる。例えば、特開昭59-16216
3 、特公平2-11542 、特公平2-7901、特公平2-7897等の
溶媒重合法が挙げられる。
The copolymer (A) of the present invention can be produced by a known method. For example, JP-A-59-16216
3, the Japanese Patent Publication No. 211542, the Japanese Patent Publication No. 2-7901, the Japanese Patent Publication No. 2-7897, etc. solvent polymerization methods.

【0019】溶媒重合法において用いる溶剤としては、
水、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、ベンゼン、トルエン、キシレン、シクロ
ヘキサン、n−ヘキサン、脂肪族炭化水素、酢酸エチ
ル、アセトン、メチルエチルケトン等が挙げられる。取
扱と反応設備から考慮すると水および1〜4級アルコー
ルが好ましい。
The solvent used in the solvent polymerization method is
Examples thereof include water, methyl alcohol, ethyl alcohol, isopropyl alcohol, benzene, toluene, xylene, cyclohexane, n-hexane, aliphatic hydrocarbons, ethyl acetate, acetone and methyl ethyl ketone. Water and primary to quaternary alcohols are preferable in consideration of handling and reaction equipment.

【0020】水系の重合開始剤としては、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
溶性の開始剤が使用される。水系以外の溶剤を用いる溶
媒重合にはベンゾイルパーオキシド、ラウロイルパーオ
キシド等が重合開始剤として使用される。
As the water-based polymerization initiator, a water-soluble initiator such as ammonium or alkali metal persulfate or hydrogen peroxide is used. Benzoyl peroxide, lauroyl peroxide and the like are used as a polymerization initiator for solvent polymerization using a solvent other than an aqueous solvent.

【0021】また、重合開始剤と併用して、促進剤とし
て亜硫酸水素ナトリウムやメルカプトエタノールやアミ
ン化合物を使用することも可能であり、これら重合開始
剤あるいは促進剤を適宜選択して用いることができる。
It is also possible to use sodium bisulfite, mercaptoethanol or an amine compound as an accelerator in combination with the polymerization initiator, and these polymerization initiators or accelerators can be appropriately selected and used. .

【0022】本発明の共重合体 (イ) の重量平均分子量
(ゲルパーミエーションクロマトグラフィー法/ポリス
チレンスルホン酸ナトリウム換算) は 3,000〜1,000,00
0 の範囲が良く、 5,000〜100,000 がより好ましい。分
子量が大きすぎると流動性が低下し、また分子量が小さ
すぎると分離抵抗性が低下傾向を示す。
Weight average molecular weight of the copolymer (a) of the present invention
(Gel permeation chromatography method / sodium polystyrene sulfonate conversion) is 3,000 to 1,000,00
A range of 0 is preferable, and 5,000 to 100,000 is more preferable. If the molecular weight is too large, the fluidity will decrease, and if the molecular weight is too small, the separation resistance will tend to decrease.

【0023】さらに本発明における共重合体 (イ) は、
本発明の効果を損なわない範囲内で他の共重合可能な単
量体と反応させてもよい。例えば、アクリロニトリル、
アクリル酸エステル、アクリルアミド、メタクリルアミ
ド、スチレン、スチレンスルホン酸等が挙げられる。
Further, the copolymer (a) in the present invention is
You may react with another copolymerizable monomer within the range which does not impair the effect of this invention. For example, acrylonitrile,
Examples thereof include acrylic acid ester, acrylamide, methacrylamide, styrene, styrene sulfonic acid and the like.

【0024】また、本発明における消泡剤 (ロ) は特に
限定するものではないが、ジメチルポリシロキサンを主
成分とするシリコン系消泡剤やポリアルキレングリコー
ル脂肪酸エステルを主成分とする消泡剤が好ましく使用
される。
The antifoaming agent (b) in the present invention is not particularly limited, but a silicon-based antifoaming agent containing dimethylpolysiloxane as a main component or an antifoaming agent containing polyalkylene glycol fatty acid ester as a main component. Is preferably used.

【0025】シリコン系消泡剤としては乳化タイプの水
と相溶性のあるものが好ましく使用される。一例を挙げ
れば、信越シリコン社製:KM-70,KM-73A等のKMシリー
ズ、東芝シリコン社製:TSA シリーズ、ダウコーニング
社製:FSアンチフォームシリーズ、花王社製:アンチフ
ォームE-20等が挙げられる。
As the silicone type defoaming agent, an emulsifying type which is compatible with water is preferably used. As an example, Shin-Etsu Silicon Co .: KM series such as KM-70, KM-73A, Toshiba Silicon Co .: TSA series, Dow Corning Co .: FS Antifoam series, Kao Co .: Antifoam E-20 etc. Is mentioned.

【0026】ポリアルキレングリコール脂肪酸エステル
を主成分とする消泡剤としては、花王社製:レオゾール
TWL120、日華化学社製:ニコフィックス、フォームレッ
クス797 等が挙げられる。
As an antifoaming agent containing a polyalkylene glycol fatty acid ester as a main component, Kao Corporation: Resol
TWL120, Nichika Chemical Co., Ltd .: Nicofix, Form Rex 797 and the like.

【0027】本発明の混和剤組成物において、共重合体
(イ) と消泡剤 (ロ) の配合比は、(イ) / (ロ) = 10
0/0.01〜5.0(固形分重量比) 程度であり、 100/0.1〜
1.0が好ましく使用される。100/0.01未満では消泡効果
が充分ではなく、100/5.0を超えると分散性が低下傾向
となる。
In the admixture composition of the present invention, the copolymer
The compounding ratio of (ii) and defoamer (ii) is (ii) / (ii) = 10
0 / 0.01 to 5.0 (solid content weight ratio), 100 / 0.1 to
1.0 is preferably used. If it is less than 100 / 0.01, the defoaming effect is not sufficient, and if it exceeds 100 / 5.0, the dispersibility tends to decrease.

【0028】本発明の共重合体 (イ) の添加量は、セメ
ントに対して固形分で0.02〜1.0 重量%程度が使用範囲
であり、 0.1〜0.5 重量%が好ましく使用される。
The addition amount of the copolymer (a) of the present invention is about 0.02 to 1.0% by weight based on the solid content of the cement, and 0.1 to 0.5% by weight is preferably used.

【0029】また、本発明の混和剤組成物の添加は、共
重合体 (イ) と消泡剤 (ロ) を予め配合したものを添加
しても、あるいは別々に添加してもよく、限定されるも
のではない。
Further, the admixture composition of the present invention may be added by premixing the copolymer (a) and the defoaming agent (b) or by adding them separately. It is not something that will be done.

【0030】本発明の混和剤組成物は、振動機による締
め固めを行うコンクリート製品の製造や、重力加速度3G
〜60G の遠心力を加えて成型するコンクリート製品の製
造に用いる。
The admixture composition of the present invention is used for the production of concrete products for compaction by a vibration machine and the acceleration of gravity of 3G.
Used to manufacture concrete products that are molded by applying a centrifugal force of ~ 60G.

【0031】更に、近年振動機を使用しない自己充填性
のコンクリートである高流動コンクリートの研究が行わ
れているが、これらのコンクリートを用いたコンクリー
ト製品の製造に混和剤組成物として用いることができ
る。ここで、高流動コンクリートとは、コンクリートが
45cm (JIS A-1101スランプ試験に準ずるフロー値) 程度
以上の流動性を示すコンクリートを表わす。
Furthermore, recently, studies have been conducted on high-fluidity concrete which is a self-filling concrete that does not use a vibrator, but it can be used as an admixture composition in the production of concrete products using these concretes. . Here, high fluidity concrete is concrete
Represents concrete that exhibits fluidity of about 45 cm (flow value based on JIS A-1101 slump test).

【0032】本発明の対象となるコンクリートは、セメ
ント、細骨材、粗骨材を主成分とするものであるが、各
種の高炉スラグ、フライアッシュ等の各種混和材料を使
用することができる。更に、公知の添加剤 (材) と併用
することができる。例えば、AE剤、AE減水剤、高性
能減水剤、遅延剤、早強剤、促進剤、起泡剤、発泡剤、
増粘剤、防水剤、防泡剤等が挙げられる。
The concrete to which the present invention is applied has cement, fine aggregate and coarse aggregate as main components, but various admixture materials such as various blast furnace slags and fly ash can be used. Furthermore, it can be used in combination with known additives (materials). For example, AE agent, AE water reducing agent, high performance water reducing agent, retarder, early strengthening agent, accelerator, foaming agent, foaming agent,
Examples thereof include thickeners, waterproofing agents, antifoaming agents and the like.

【0033】[0033]

【実施例】以下、本発明を具体的に説明するが、本発明
はこれらの実施例に限定されるものではない。尚、以下
の例における「%」は、特にことわりのない限り、「重
量%」である。
EXAMPLES The present invention will be specifically described below, but the present invention is not limited to these examples. In addition, "%" in the following examples is "% by weight" unless otherwise specified.

【0034】また、実施例中で示す共重合体 (イ) の平
均分子量はゲルパーミエーションクロマトグラフィー法
/ポリスチレンスルホン酸ナトリウム換算による分子量
から求めたものである。
Further, the average molecular weight of the copolymer (a) shown in the examples is obtained from the gel permeation chromatography method / molecular weight in terms of sodium polystyrene sulfonate.

【0035】本発明の重合に使用した単量体(a) の内容
と記号を以下に示す。但し、EOはエチレンオキシド、PO
はプロピレンオキシドを表す。
The contents and symbols of the monomer (a) used in the polymerization of the present invention are shown below. However, EO is ethylene oxide, PO
Represents propylene oxide.

【0036】A−1:メタノールEO・メタクリル酸モノ
エステル (EO付加モル数=115) A−2:メタノールEO・アクリル酸モノエステル (EO付
加モル数=220) A−3:メタノールEO・メタクリル酸モノエステル (EO
付加モル数=280) A−4:アクリル酸EO付加物 (EO付加モル数=130) A−5:アクリル酸PO・EOブロック付加物(PO付加モ
ル数=10・EO付加モル数=135) A−6:アクリル酸EO・POブロック付加物(EO付加モル
数=135・PO付加モル数=5) A−7:メタノールEO・メタクリル酸モノエステル (EO
付加モル数=23)(比較) A−8:メタノールEO・メタクリル酸モノエステル (EO
付加モル数=102)(比較) A−9:メタノールEO・メタクリル酸モノエステル (EO
付加モル数=350)(比較) 。
A-1: Methanol EO / methacrylic acid monoester (EO addition mole number = 115) A-2: Methanol EO / acrylic acid monoester (EO addition mole number = 220) A-3: Methanol EO / methacrylic acid Monoester (EO
Addition mol number = 280) A-4: Acrylic acid EO adduct (EO addition mol number = 130) A-5: Acrylic acid PO / EO block adduct (PO addition mol number = 10 / EO addition mol number = 135) A-6: Acrylic acid EO / PO block addition product (EO addition mole number = 135 / PO addition mole number = 5) A-7: Methanol EO / methacrylic acid monoester (EO
Addition mol number = 23) (Comparison) A-8: Methanol EO / methacrylic acid monoester (EO
Addition mol number = 102) (Comparison) A-9: Methanol EO / methacrylic acid monoester (EO
Number of added moles = 350) (comparison).

【0037】以下に共重合体 (イ) の製造例を示す。製造例1 (混和剤の記号C−1) 攪拌機付き反応容器に水10モルを仕込み、攪拌しながら
窒素置換し、窒素雰囲気中で75℃まで昇温した。A−1
0.09 モルとアクリル酸1モル (モル比=9/100)、水
7.5モルを混合溶解したものと20%過硫酸アンモニウム
水溶液0.01モル、及び2−メルカプトエタノール4gの
3者をそれぞれ同時に反応系に2時間かけて滴下する。
次に20%過硫酸アンモニウム水溶液0.03モルを30分かけ
て滴下し、1時間同温度 (75℃) で熟成する。熟成後95
℃に昇温して、35%過酸化水素12gを1時間かけて滴下
し、2時間同温度 (95℃) で熟成する。熟成終了後、48
%水酸化ナトリウム 0.7モルを加えて中和、分子量22,0
00の共重合体を得た。
The production examples of the copolymer (a) are shown below. Production Example 1 (Symbol C-1 for admixture) 10 mol of water was charged into a reaction vessel equipped with a stirrer, the atmosphere was replaced with nitrogen while stirring, and the temperature was raised to 75 ° C in a nitrogen atmosphere. A-1
0.09 mol and acrylic acid 1 mol (molar ratio = 9/100), water
A mixture of 7.5 mol, 0.01 mol of a 20% aqueous solution of ammonium persulfate, and 4 g of 2-mercaptoethanol were added dropwise to the reaction system simultaneously over 2 hours.
Next, 0.03 mol of 20% ammonium persulfate aqueous solution is added dropwise over 30 minutes, and the mixture is aged at the same temperature (75 ° C) for 1 hour. After aging 95
The temperature is raised to ℃, 12g of 35% hydrogen peroxide is added dropwise over 1 hour, and the mixture is aged at the same temperature (95 ℃) for 2 hours. After aging, 48
Add 0.7 mol% sodium hydroxide to neutralize, molecular weight 22,0
A copolymer of 00 was obtained.

【0038】製造例2 (混和剤の記号C−2) 攪拌機付き反応容器に水8モルを仕込み、攪拌しながら
窒素置換し、窒素雰囲気中で75℃まで昇温した。A−2
0.05 モルとメタクリル酸1モル (モル比=5/100)、水
8.5モルを混合溶解したものと20%過硫酸アンモニウム
水溶液0.01モル、及び2−メルカプトエタノール3gの
3者をそれぞれ同時に反応系に2時間かけて滴下する。
次に20%過硫酸アンモニウム水溶液0.03モルを30分かけ
て滴下し、1時間同温度 (75℃) で熟成する。熟成後95
℃に昇温して、35%過酸化水素9gを1時間かけて滴下
し、2時間同温度 (95℃) で熟成する。熟成終了後、48
%水酸化ナトリウム 0.7モルを加えて中和、分子量85,0
00の共重合体を得た。
Production Example 2 (Symbol C-2 for admixture) 8 mol of water was charged into a reaction vessel equipped with a stirrer, the atmosphere was replaced with nitrogen while stirring, and the temperature was raised to 75 ° C. in a nitrogen atmosphere. A-2
0.05 mol and 1 mol of methacrylic acid (molar ratio = 5/100), water
A mixture of 8.5 mol, 0.01 mol of a 20% ammonium persulfate aqueous solution, and 3 g of 2-mercaptoethanol were simultaneously added dropwise to the reaction system over 2 hours.
Next, 0.03 mol of 20% ammonium persulfate aqueous solution is added dropwise over 30 minutes, and the mixture is aged at the same temperature (75 ° C) for 1 hour. After aging 95
The temperature is raised to 0 ° C., 9 g of 35% hydrogen peroxide is added dropwise over 1 hour, and the mixture is aged at the same temperature (95 ° C.) for 2 hours. After aging, 48
Add 0.7 mol% sodium hydroxide to neutralize, molecular weight 85,0
A copolymer of 00 was obtained.

【0039】製造例3 (混和剤の記号C−3) 攪拌機付き反応容器に水5モルを仕込み、攪拌しながら
窒素置換し、窒素雰囲気中で95℃まで昇温した。A−3
0.002モルとマレイン酸モノナトリウム塩1モル (モル
比=0.2/100)、90℃温水15モルを混合溶解したものと20
%過硫酸アンモニウム水溶液0.01モル、及び2−メルカ
プトエタノール3gの3者をそれぞれ同時に反応系に2
時間かけて滴下する。次に20%過硫酸アンモニウム水溶
液0.03モルを30分かけて滴下し、1時間同温度 (95℃)
で熟成する。熟成後95℃で35%過酸化水素9gを1時間
かけて滴下し、2時間同温度 (95℃) で熟成する。熟成
終了後、48%水酸化ナトリウム 0.7モルを加えて中和、
分子量12,000の共重合体を得た。
Production Example 3 (Symbol C-3 for admixture) 5 mol of water was charged into a reaction vessel equipped with a stirrer, the atmosphere was replaced with nitrogen while stirring, and the temperature was raised to 95 ° C in a nitrogen atmosphere. A-3
20 with a mixture of 0.002 mol, 1 mol of maleic acid monosodium salt (molar ratio = 0.2 / 100), and 15 mol of 90 ° C warm water
% Mol ammonium persulfate aqueous solution 0.01 mol, and 2-mercaptoethanol 3 g simultaneously into the reaction system
Drop over time. Next, 0.03 mol of 20% ammonium persulfate aqueous solution was added dropwise over 30 minutes, and the temperature was kept at the same temperature (95 ° C) for 1 hour.
Mature in. After aging, 9% of 35% hydrogen peroxide was added dropwise at 95 ° C over 1 hour, and the mixture was aged at the same temperature (95 ° C) for 2 hours. After aging, add 0.7 mol of 48% sodium hydroxide to neutralize,
A copolymer having a molecular weight of 12,000 was obtained.

【0040】製造例4 (混和剤の記号C−4) 攪拌機付き反応容器に水10モルを仕込み、攪拌しながら
窒素置換し、窒素雰囲気中で75℃まで昇温した。A−4
0.01 モルとアクリル酸 0.9モルとメタリルスルホン酸
ナトリウム 0.1モル (モル比=1/90/10)、水 7.5モルを
混合溶解したものと20%過硫酸アンモニウム水溶液0.01
モル、及び2−メルカプトエタノール4gの3者をそれ
ぞれ同時に反応系に2時間かけて滴下する。次に20%過
硫酸アンモニウム水溶液0.03モルを30分かけて滴下し、
1時間同温度 (75℃) で熟成する。熟成後95℃に昇温し
て、35%過酸化水素12gを1時間かけて滴下し、2時間
同温度 (95℃) で熟成する。熟成終了後、48%水酸化ナ
トリウム 0.6モルを加えて中和、分子量 7,200の共重合
体を得た。
Production Example 4 (Symbol C-4 of admixture) 10 mol of water was charged into a reaction vessel equipped with a stirrer, the atmosphere was replaced with nitrogen while stirring, and the temperature was raised to 75 ° C in a nitrogen atmosphere. A-4
A mixture of 0.01 mol, 0.9 mol of acrylic acid, 0.1 mol of sodium methallyl sulfonate (molar ratio = 1/90/10) and 7.5 mol of water and dissolved, and a 20% ammonium persulfate aqueous solution 0.01
Mol and 2-mercaptoethanol (4 g) are simultaneously added dropwise to the reaction system over 2 hours. Next, 0.03 mol of 20% ammonium persulfate aqueous solution was added dropwise over 30 minutes,
Aging at the same temperature (75 ℃) for 1 hour. After aging, the temperature is raised to 95 ° C., 12 g of 35% hydrogen peroxide is added dropwise over 1 hour, and aging is performed at the same temperature (95 ° C.) for 2 hours. After completion of aging, 0.6 mol of 48% sodium hydroxide was added for neutralization to obtain a copolymer having a molecular weight of 7,200.

【0041】製造例5 (混和剤の記号C−5) 攪拌機付き反応容器に水10モルを仕込み、攪拌しながら
窒素置換し、窒素雰囲気中で75℃まで昇温した。A−5
0.01 モルとメタクリル酸1モル (モル比=1/100)、水
7.5モルを混合溶解したものと20%過硫酸アンモニウム
水溶液0.01モル、及び2−メルカプトエタノール1gの
3者をそれぞれ同時に反応系に2時間かけて滴下する。
次に20%過硫酸アンモニウム水溶液0.03モルを30分かけ
て滴下し、1時間同温度 (75℃) で熟成する。熟成後95
℃に昇温して、35%過酸化水素5gを1時間かけて滴下
し、2時間同温度 (95℃) で熟成する。熟成終了後、48
%水酸化ナトリウム 0.7モルを加えて中和、分子量105,
000 の共重合体を得た。
Production Example 5 (Symbol C-5) A reaction vessel equipped with a stirrer was charged with 10 mol of water, the atmosphere was replaced with nitrogen while stirring, and the temperature was raised to 75 ° C. in a nitrogen atmosphere. A-5
0.01 mol and 1 mol of methacrylic acid (molar ratio = 1/100), water
A mixture of 7.5 mol, 0.01 mol of a 20% aqueous solution of ammonium persulfate, and 1 g of 2-mercaptoethanol are simultaneously added dropwise to the reaction system over 2 hours.
Next, 0.03 mol of 20% ammonium persulfate aqueous solution is added dropwise over 30 minutes, and the mixture is aged at the same temperature (75 ° C) for 1 hour. After aging 95
The temperature is raised to 0 ° C., 5 g of 35% hydrogen peroxide is added dropwise over 1 hour, and the mixture is aged at the same temperature (95 ° C.) for 2 hours. After aging, 48
Add 0.7 mol% sodium hydroxide to neutralize, molecular weight 105,
000 copolymers were obtained.

【0042】製造例6 (混和剤の記号C−6) 攪拌機付き反応容器に水10モルを仕込み、攪拌しながら
窒素置換し、窒素雰囲気中で75℃まで昇温した。A−6
0.01 モルとアクリル酸ナトリウム1モル (モル比=1/
100)、水 7.5モルを混合溶解したものと20%過硫酸アン
モニウム水溶液0.01モル、及び2−メルカプトエタノー
ル2gの3者をそれぞれ同時に反応系に2時間かけて滴
下する。次に20%過硫酸アンモニウム水溶液0.03モルを
30分かけて滴下し、1時間同温度 (75℃) で熟成する。
熟成後95℃に昇温して、35%過酸化水素9gを1時間か
けて滴下し、2時間同温度 (95℃) で熟成する。熟成終
了後、48%水酸化ナトリウム 0.7モルを加えて中和、分
子量77,000の共重合体を得た。
Production Example 6 (Symbol C-6 as an admixture) 10 mol of water was charged into a reaction vessel equipped with a stirrer, the atmosphere was replaced with nitrogen while stirring, and the temperature was raised to 75 ° C in a nitrogen atmosphere. A-6
0.01 mol and 1 mol of sodium acrylate (molar ratio = 1 /
100), 7.5 mol of water mixed and dissolved, 0.01 mol of 20% ammonium persulfate aqueous solution, and 2 g of 2-mercaptoethanol are simultaneously added dropwise to the reaction system over 2 hours. Next, 0.03 mol of 20% ammonium persulfate aqueous solution
Drop over 30 minutes and age for 1 hour at the same temperature (75 ° C).
After aging, the temperature is raised to 95 ° C., 9 g of 35% hydrogen peroxide is added dropwise over 1 hour, and aging is performed at the same temperature (95 ° C.) for 2 hours. After the aging was completed, 48 mol of sodium hydroxide (0.7 mol) was added for neutralization to obtain a copolymer having a molecular weight of 77,000.

【0043】製造例7 (混和剤の記号C−7) 攪拌機付き反応容器に水23モルを仕込み、攪拌しながら
窒素置換し、窒素雰囲気中で75℃まで昇温した。A−2
0.045モルとアクリル酸 0.3モル (モル比=15/100) 、
水10モルを混合溶解したものと20%過硫酸アンモニウム
水溶液 0.003モル、及び2−メルカプトエタノール 1.2
gの3者をそれぞれ同時に反応系に2時間かけて滴下す
る。次に20%過硫酸アンモニウム水溶液 0.009モルを30
分かけて滴下し、1時間同温度 (75℃) で熟成する。熟
成後95℃に昇温して、35%過酸化水素4gを1時間かけ
て滴下し、2時間同温度 (95℃) で熟成する。熟成終了
後、48%水酸化ナトリウム0.21モルを加えて中和、分子
量51,000の共重合体を得た。
Production Example 7 (Symbol C-7 as an admixture) 23 mol of water was placed in a reaction vessel equipped with a stirrer, the atmosphere was replaced with nitrogen while stirring, and the temperature was raised to 75 ° C in a nitrogen atmosphere. A-2
0.045 mol and acrylic acid 0.3 mol (molar ratio = 15/100),
A mixture of 10 mol of water and 0.003 mol of 20% ammonium persulfate aqueous solution, and 2-mercaptoethanol 1.2.
g of each of the three is simultaneously added dropwise to the reaction system over 2 hours. Next, 0.009 mol of a 20% ammonium persulfate aqueous solution is added to 30%.
Drop over a period of minutes and age for 1 hour at the same temperature (75 ° C). After aging, the temperature is raised to 95 ° C., 4 g of 35% hydrogen peroxide is added dropwise over 1 hour, and aging is performed at the same temperature (95 ° C.) for 2 hours. After the completion of aging, 0.21 mol of 48% sodium hydroxide was added for neutralization to obtain a copolymer having a molecular weight of 51,000.

【0044】製造例8 (混和剤の記号C−8) 攪拌機付き反応容器に水23モルを仕込み、攪拌しなが
ら窒素置換し、窒素雰囲気中で75℃まで昇温した。A−
1 0.08 モルとアクリル酸 0.2モル (モル比=40/100)
、水12モルを混合溶解したものと20%過硫酸アンモニ
ウム水溶液 0.002モル、及び2−メルカプトエタノール
0.6gの3者をそれぞれ同時に反応系に2時間かけて滴
下する。次に20%過硫酸アンモニウム水溶液 0.006モル
を30分かけて滴下し、1時間同温度 (75℃) で熟成す
る。熟成後95℃に昇温して、35%過酸化水素3gを1時
間かけて滴下し、2時間同温度 (95℃) で熟成する。熟
成終了後、48%水酸化ナトリウム0.14モルを加えて中
和、分子量56,000の共重合体を得た。
Production Example 8 (Symbol C-8 as an admixture) 23 mol of water was charged into a reaction vessel equipped with a stirrer, the atmosphere was replaced with nitrogen while stirring, and the temperature was raised to 75 ° C in a nitrogen atmosphere. A-
1 0.08 mol and acrylic acid 0.2 mol (molar ratio = 40/100)
, A mixture of 12 mol of water and 0.002 mol of 20% ammonium persulfate aqueous solution, and 2-mercaptoethanol
0.6 g of each of the three substances is dropped simultaneously into the reaction system over 2 hours. Next, 0.006 mol of a 20% ammonium persulfate aqueous solution is added dropwise over 30 minutes, and the mixture is aged at the same temperature (75 ° C) for 1 hour. After aging, the temperature is raised to 95 ° C., 3 g of 35% hydrogen peroxide is added dropwise over 1 hour, and aging is performed at the same temperature (95 ° C.) for 2 hours. After the aging was completed, 0.14 mol of 48% sodium hydroxide was added to neutralize and obtain a copolymer having a molecular weight of 56,000.

【0045】製造例9 (混和剤の記号C−9) 攪拌機付き反応容器に水18モルを仕込み、攪拌しながら
窒素置換し、窒素雰囲気中で75℃まで昇温した。A−1
0.06 モルとアクリル酸 0.1モル (モル比=60/100) 、
水8モルを混合溶解したものと20%過硫酸アンモニウム
水溶液 0.001モル、及び2−メルカプトエタノール 0.3
gの3者をそれぞれ同時に反応系に2時間かけて滴下す
る。次に20%過硫酸アンモニウム水溶液 0.003モルを30
分かけて滴下し、1時間同温度 (75℃) で熟成する。熟
成後95℃に昇温して、35%過酸化水素2gを1時間かけ
て滴下し、2時間同温度 (95℃) で熟成する。熟成終了
後、48%水酸化ナトリウム0.07モルを加えて中和、分子
量45,000の共重合体を得た。
Production Example 9 (symbol C-9 as an admixture) 18 mol of water was charged into a reaction vessel equipped with a stirrer, the atmosphere was replaced with nitrogen while stirring, and the temperature was raised to 75 ° C in a nitrogen atmosphere. A-1
0.06 mol and acrylic acid 0.1 mol (molar ratio = 60/100),
A mixture of 8 moles of water, 0.001 mole of 20% aqueous ammonium persulfate solution, and 2-mercaptoethanol 0.3
g of each of the three is simultaneously added dropwise to the reaction system over 2 hours. Next, 0.003 mol of 20% ammonium persulfate aqueous solution is added to 30%.
Drop over a period of minutes and age for 1 hour at the same temperature (75 ° C). After aging, the temperature is raised to 95 ° C., 2 g of 35% hydrogen peroxide is added dropwise over 1 hour, and aging is performed at the same temperature (95 ° C.) for 2 hours. After completion of the aging, 0.07 mol of 48% sodium hydroxide was added for neutralization to obtain a copolymer having a molecular weight of 45,000.

【0046】製造例10 (混和剤の記号C−10) 攪拌機付き反応容器に水30モルを仕込み、攪拌しながら
窒素置換し、窒素雰囲気中で75℃まで昇温した。A−1
0.1モルとアクリル酸 0.1モル (モル比=100/100)、水
13モルを混合溶解したものと20%過硫酸アンモニウム水
溶液 0.001モル、及び2−メルカプトエタノール 0.3g
の3者をそれぞれ同時に反応系に2時間かけて滴下す
る。次に20%過硫酸アンモニウム水溶液 0.003モルを30
分かけて滴下し、1時間同温度 (75℃) で熟成する。熟
成後95℃に昇温して、35%過酸化水素2gを1時間かけ
て滴下し、2時間同温度 (95℃) で熟成する。熟成終了
後、48%水酸化ナトリウム0.07モルを加えて中和、分子
量72,000の共重合体を得た。
Production Example 10 (symbol C-10 as an admixture) 30 mol of water was charged into a reaction vessel equipped with a stirrer, the atmosphere was replaced with nitrogen while stirring, and the temperature was raised to 75 ° C in a nitrogen atmosphere. A-1
0.1 mol and acrylic acid 0.1 mol (molar ratio = 100/100), water
A mixture of 13 mol and dissolved, 0.001 mol of 20% ammonium persulfate aqueous solution, and 0.3 g of 2-mercaptoethanol
Each of the three is simultaneously added dropwise to the reaction system over 2 hours. Next, 0.003 mol of 20% ammonium persulfate aqueous solution is added to 30%.
Drop over a period of minutes and age for 1 hour at the same temperature (75 ° C). After aging, the temperature is raised to 95 ° C., 2 g of 35% hydrogen peroxide is added dropwise over 1 hour, and aging is performed at the same temperature (95 ° C.) for 2 hours. After completion of the aging, 0.07 mol of 48% sodium hydroxide was added for neutralization to obtain a copolymer having a molecular weight of 72,000.

【0047】製造例11 (混和剤の記号C−11) 攪拌機付き反応容器に水10モルを仕込み、攪拌しながら
窒素置換し、窒素雰囲気中で75℃まで昇温した。A−7
0.1モルとアクリル酸1モル (モル比=10/100) 、水
7.5モルを混合溶解したものと20%過硫酸アンモニウム
水溶液0.01モル、及び2−メルカプトエタノール4gの
3者をそれぞれ同時に反応系に2時間かけて滴下する。
次に20%過硫酸アンモニウム水溶液0.03モルを30分かけ
て滴下し、1時間同温度 (75℃) で熟成する。熟成後95
℃に昇温して、35%過酸化水素12gを1時間かけて滴下
し、2時間同温度 (95℃) で熟成する。熟成終了後、48
%水酸化ナトリウム 0.7モルを加えて中和、分子量11,0
00の共重合体を得た。
Production Example 11 (Symbol C-11 for admixture) 10 mol of water was charged into a reaction vessel equipped with a stirrer, the atmosphere was replaced with nitrogen while stirring, and the temperature was raised to 75 ° C in a nitrogen atmosphere. A-7
0.1 mol and acrylic acid 1 mol (molar ratio = 10/100), water
A mixture of 7.5 mol, 0.01 mol of a 20% aqueous solution of ammonium persulfate, and 4 g of 2-mercaptoethanol were added dropwise to the reaction system simultaneously over 2 hours.
Next, 0.03 mol of 20% ammonium persulfate aqueous solution is added dropwise over 30 minutes, and the mixture is aged at the same temperature (75 ° C) for 1 hour. After aging 95
The temperature is raised to ℃, 12g of 35% hydrogen peroxide is added dropwise over 1 hour, and the mixture is aged at the same temperature (95 ℃) for 2 hours. After aging, 48
Add 0.7 mol% sodium hydroxide to neutralize, molecular weight 11,0
A copolymer of 00 was obtained.

【0048】製造例12 (混和剤の記号C−12) 攪拌機付き反応容器に水10モルを仕込み、攪拌しながら
窒素置換し、窒素雰囲気中で75℃まで昇温した。A−8
0.05 モルとアクリル酸1モル (モル比=5/100)、水
7.5モルを混合溶解したものと20%過硫酸アンモニウム
水溶液0.01モル、及び2−メルカプトエタノール3gの
3者をそれぞれ同時に反応系に2時間かけて滴下する。
次に20%過硫酸アンモニウム水溶液0.03モルを30分かけ
て滴下し、1時間同温度 (75℃) で熟成する。熟成後95
℃に昇温して、35%過酸化水素10gを1時間かけて滴下
し、2時間同温度 (95℃) で熟成する。熟成終了後、48
%水酸化ナトリウム 0.7モルを加えて中和、分子量31,0
00の共重合体を得た。
Production Example 12 (symbol C-12 as an admixture) 10 mol of water was charged into a reaction vessel equipped with a stirrer, the atmosphere was replaced with nitrogen while stirring, and the temperature was raised to 75 ° C in a nitrogen atmosphere. A-8
0.05 mol and acrylic acid 1 mol (molar ratio = 5/100), water
A mixture of 7.5 mol, 0.01 mol of a 20% ammonium persulfate aqueous solution, and 3 g of 2-mercaptoethanol are simultaneously added dropwise to the reaction system over 2 hours.
Next, 0.03 mol of 20% ammonium persulfate aqueous solution is added dropwise over 30 minutes, and the mixture is aged at the same temperature (75 ° C) for 1 hour. After aging 95
The temperature is raised to 10 ° C., 10 g of 35% hydrogen peroxide is added dropwise over 1 hour, and the mixture is aged at the same temperature (95 ° C.) for 2 hours. After aging, 48
Add 0.7 mol% sodium hydroxide to neutralize, molecular weight 31,0
A copolymer of 00 was obtained.

【0049】製造例13 (混和剤の記号C−13) 攪拌機付き反応容器に水5モルを仕込み、攪拌しながら
窒素置換し、窒素雰囲気中で95℃まで昇温した。A−9
0.005モルとアクリル酸1モル (モル比=0.5/100)、75
℃温水15モルを混合溶解したものと20%過硫酸アンモニ
ウム水溶液0.01モル、及び2−メルカプトエタノール3
gの3者をそれぞれ同時に反応系に2時間かけて滴下す
る。次に20%過硫酸アンモニウム水溶液0.03モルを30分
かけて滴下し、1時間同温度 (95℃) で熟成する。熟成
後95℃で35%過酸化水素9gを1時間かけて滴下し、2
時間同温度 (95℃) で熟成する。熟成終了後、48%水酸
化ナトリウム 0.7モルを加えて中和、分子量25,000の共
重合体を得た。
Production Example 13 (Symbol C-13 of admixture) 5 mol of water was charged into a reaction vessel equipped with a stirrer, the atmosphere was replaced with nitrogen while stirring, and the temperature was raised to 95 ° C in a nitrogen atmosphere. A-9
0.005 mol and acrylic acid 1 mol (molar ratio = 0.5 / 100), 75
Mixture of 15 mol of warm water, 0.01 mol of 20% ammonium persulfate aqueous solution, and 2-mercaptoethanol 3
g of each of the three is simultaneously added dropwise to the reaction system over 2 hours. Next, 0.03 mol of a 20% ammonium persulfate aqueous solution is added dropwise over 30 minutes, followed by aging at the same temperature (95 ° C) for 1 hour. After aging, add 9 g of 35% hydrogen peroxide at 95 ° C over 1 hour, and add 2
Aging at the same temperature (95 ℃) for a certain period of time. After completion of the aging, 0.7 mol of 48% sodium hydroxide was added to neutralize and obtain a copolymer having a molecular weight of 25,000.

【0050】共重合体の比較重合物の他に、実施例に使
用した比較混和剤の内容と記号を以下に示す。 混和剤の記号NS:ナフタレン系混和剤 (マイテイ150
; 花王(株)製) 混和剤の記号MS:メラミン系混和剤 (マイテイ150V-
2;花王(株)製) 。
The contents and symbols of the comparative admixtures used in the examples are shown below, in addition to the comparative polymer of the copolymer. Symbol for admixture NS: Naphthalene admixture (Mighty 150
; Kao Corporation) Admixture symbol MS: Melamine admixture (Mighty 150V-
2; manufactured by Kao Corporation.

【0051】実施例に使用した消泡剤 (ロ) の内容と記
号を表1に示す。
Table 1 shows the contents and symbols of the defoaming agent (b) used in the examples.

【0052】[0052]

【表1】 [Table 1]

【0053】コンクリート試験の評価方法 コンクリートの配合条件を表2〜4に示す。尚、表2は
振動締め固めコンクリート製品用配合、表3は遠心力締
め固めコンクリート製品用配合、表4は高流動コンクリ
ート製品用配合を表わす。
Evaluation Method of Concrete Test Tables 2 to 4 show concrete mixing conditions. Table 2 shows the composition for vibration compaction concrete products, Table 3 shows the composition for centrifugal compaction concrete products, and Table 4 shows the composition for high flow concrete products.

【0054】[0054]

【表2】 [Table 2]

【0055】[0055]

【表3】 [Table 3]

【0056】[0056]

【表4】 [Table 4]

【0057】1.振動締め固めコンクリート製品の評価 表2に示すコンクリート配合で本発明の混和剤組成物と
比較混和剤を添加してスランプ値を10±1cmに調整し
た。その後、マシン油を剥離剤として塗布した直径15c
m、高さ30cmの円柱型枠にコンクリートを詰め、テーブ
ルバイブレーターにて15秒間振動充填を行い、試験体を
成型した。硬化後のコンクリート表面にある直径2mm以
上の気泡の個数を100cm2の面積について数えて表面美観
性を次のように判定した。 ○ − 4個以下 △ − 5〜19個 × − 20個以上 更に、JIS A 1101法によりコンクリート製造直後のスラ
ンプ値を測定した。試験結果を表5に示す。
1. Evaluation of vibration compacted concrete product The slump value was adjusted to 10 ± 1 cm by adding the admixture composition of the present invention and the comparative admixture in the concrete composition shown in Table 2. After that, machine oil is applied as a release agent with a diameter of 15c
Concrete was packed in a cylindrical mold having a height of 30 cm and a height of 30 cm, and vibration filling was performed for 15 seconds using a table vibrator to mold a test body. The number of bubbles having a diameter of 2 mm or more on the surface of the concrete after hardening was counted for an area of 100 cm 2 , and the surface aesthetics was judged as follows. ○ -4 or less △ -5 to 19 × -20 or more Further, the slump value immediately after concrete production was measured by the JIS A 1101 method. The test results are shown in Table 5.

【0058】[0058]

【表5】 [Table 5]

【0059】2.遠心締め固めコンクリート製品の評価 表3に示すコンクリート配合で、本発明の混和剤組成物
と比較混和剤を添加してスランプ値を3±1cmに調整し
た。その後、φ20cm、高さ30cmの遠心成型用型枠にコン
クリートを13kg投入して、遠心締め固めを行った。締め
固め時間による硬化コンクリートの強度測定とコンクリ
ートの締まり程度を肉眼で観察した。遠心条件は重力加
速度5Gで1分、次いで 15Gで2分、次いで 30Gで2分
後、4分後、6分後の締まり程度を測定した。 コンクリートの締まり程度 ○ − 平滑的に締まっている。 △ − 内面または外面の平滑性がやや悪い。 × − 砂利が露出し、内面または外面の平滑性が著し
く悪い。 更に、スランプ値と圧縮強度を以下のように測定した。 ・スランプ値:JIS A 1101法によりコンクリート製造直
後の値を測定した。 ・圧縮強度:直径10cm、高さ20cmの円筒上供試体を作成
し、28日後の強度をJISA 1108法にて測定した。測定結
果を表6に示す。
2. Evaluation of Centrifugal Compacted Concrete Product With the concrete composition shown in Table 3, the admixture composition of the present invention and a comparative admixture were added to adjust the slump value to 3 ± 1 cm. Then, 13 kg of concrete was put into a centrifugal molding form having a diameter of 20 cm and a height of 30 cm, and centrifugal compaction was performed. The strength of the hardened concrete was measured by the compaction time and the degree of compaction of the concrete was visually observed. The centrifugal conditions were as follows: gravity acceleration of 5 G for 1 minute, 15 G for 2 minutes, 30 G for 2 minutes, 4 minutes, and 6 minutes. Degree of concrete tightening ○ − Smoothly tightened. △ -Slightly poor smoothness on the inner or outer surface. × -Exposed gravel and the inner or outer surface is extremely poor in smoothness. Further, the slump value and the compressive strength were measured as follows. -Slump value: The value immediately after concrete production was measured by the JIS A 1101 method. -Compressive strength: A cylindrical specimen having a diameter of 10 cm and a height of 20 cm was prepared, and the strength after 28 days was measured by the JIS A 1108 method. The measurement results are shown in Table 6.

【0060】[0060]

【表6】 [Table 6]

【0061】3.高流動コンクリート製品の評価 表4に示すコンクリート配合で本発明の混和剤組成物と
比較混和剤を添加してスランプ値55±5cmに調整した。
その後、マシン油を剥離剤として塗布した直径15cm、高
さ30cmの円柱型枠にコンクリートを詰め、試験体を成型
した。硬化後のコンクリート表面にある直径2mm以上の
気泡の個数を100cm2の面積について数えて表面美観性を
次のように判定した。 ○ − 4個以下 △ − 5〜19個 × − 20個以上 更に、JIS A 1101法によりコンクリート製造直後のスラ
ンプ値を測定した。試験結果を表7に示す。
3. Evaluation of high-fluidity concrete products The admixture composition of the present invention and the comparative admixture were added in the concrete composition shown in Table 4 to adjust the slump value to 55 ± 5 cm.
Then, concrete was filled into a cylindrical mold having a diameter of 15 cm and a height of 30 cm coated with machine oil as a release agent, and a test body was molded. The number of bubbles having a diameter of 2 mm or more on the surface of the concrete after hardening was counted for an area of 100 cm 2 , and the surface aesthetics was judged as follows. ○ -4 or less △ -5 to 19 × -20 or more Further, the slump value immediately after concrete production was measured by the JIS A 1101 method. The test results are shown in Table 7.

【0062】[0062]

【表7】 [Table 7]

【0063】評価結果 表5、7で明らかなように、本発明の混和剤組成物から
製造された硬化コンクリートは表面気泡の低減が顕著で
あり、表面美観が著しく改善される。また、表6で明ら
かなように遠心時間の短縮が可能となる。従って、表面
気泡の補修不要、遠心時間の短縮が可能となり、生産の
合理化が計れるものである。
Evaluation Results As is clear from Tables 5 and 7, the hardened concrete produced from the admixture composition of the present invention is remarkably reduced in surface bubbles, and the surface aesthetic appearance is remarkably improved. Further, as is clear from Table 6, the centrifugation time can be shortened. Therefore, it is possible to rationalize the production because it is not necessary to repair surface bubbles and the centrifugation time can be shortened.

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】 下記の一般式(A) で表される単量体(a)
と下記の一般式(B)及び(C) で表される化合物の中から
選ばれる1種以上の単量体(b) とを重合して得られる共
重合体 (イ) および消泡剤 (ロ) を必須成分とするコン
クリート製品用混和剤組成物。 【化1】 (式中、R1, R2:水素、メチル基 m1 :0〜2の整数 AO :炭素数2〜3のオキシアルキレン基 n : 110〜300 の整数 X :水素または炭素数1〜3のアルキル基 を表す。) 【化2】 (式中、R3〜R5 :水素、メチル基、(CH2)m2COOM2 R6 :水素、メチル基 M1,M2,Y :水素、アルカリ金属、アルカリ土類金属、ア
ンモニウム、アルキルアンモニウムまたは置換アルキル
アンモニウム m2 :0〜2の整数 を表す。)
1. A monomer (a) represented by the following general formula (A):
And a copolymer (a) obtained by polymerizing a monomer (b) selected from the compounds represented by the following general formulas (B) and (C), and an antifoaming agent ( (B) An admixture composition for concrete products, which contains (b) as an essential component. Embedded image (In the formula, R 1 and R 2 : hydrogen, a methyl group m 1 : an integer of 0 to 2 AO: an oxyalkylene group having 2 to 3 carbon atoms n: an integer of 110 to 300 X: hydrogen or a carbon number of 1 to 3 Represents an alkyl group.) (In the formula, R 3 to R 5 : hydrogen, methyl group, (CH 2 ) m 2 COOM 2 R 6 : hydrogen, methyl group M 1 , M 2 , Y: hydrogen, alkali metal, alkaline earth metal, ammonium, (Alkyl ammonium or substituted alkyl ammonium m 2 : represents an integer of 0 to 2. )
【請求項2】 共重合体 (イ) を構成する単量体(a) 、
単量体(b) の反応単位が、単量体(a) /単量体(b) =
0.1/100 〜 100/100(モル比) である請求項1記載の
コンクリート製品用混和剤組成物。
2. A monomer (a) constituting the copolymer (a),
The reaction unit of monomer (b) is monomer (a) / monomer (b) =
The admixture composition for concrete products according to claim 1, which has a molar ratio of 0.1 / 100 to 100/100.
【請求項3】 共重合体 (イ) の重量平均分子量 (ゲル
パーミエーションクロマトグラフィー法/ポリスチレン
スルホン酸ナトリウム換算) が 3,000〜1,000,000 であ
る請求項1又は2記載のコンクリート製品用混和剤組成
物。
3. The admixture composition for concrete products according to claim 1, wherein the copolymer (a) has a weight average molecular weight (gel permeation chromatography method / sodium polystyrene sulfonate conversion) of 3,000 to 1,000,000.
【請求項4】 共重合体 (イ) と消泡剤 (ロ) の配合比
が、 (イ) / (ロ)= 100/0.01〜5.0(固形分重量比)
である請求項1〜3の何れか1項に記載のコンクリート
製品用混和剤組成物。
4. The blending ratio of the copolymer (a) and the defoaming agent (b) is (a) / (b) = 100 / 0.01 to 5.0 (solid content weight ratio).
The admixture composition for concrete products according to any one of claims 1 to 3.
【請求項5】 消泡剤 (ロ) の主成分がジメチルポリシ
ロキサンである請求項1〜4の何れか1項に記載のコン
クリート製品用混和剤組成物。
5. The admixture composition for concrete products according to any one of claims 1 to 4, wherein the main component of the defoaming agent (b) is dimethylpolysiloxane.
【請求項6】 消泡剤 (ロ) の主成分がポリアルキレン
グリコール脂肪酸エステルである請求項1〜4の何れか
1項に記載のコンクリート製品用混和剤組成物。
6. The admixture composition for concrete products according to any one of claims 1 to 4, wherein a main component of the defoaming agent (b) is a polyalkylene glycol fatty acid ester.
【請求項7】 振動機による締め固めを行うコンクリー
ト製品の製造に用いることを特徴とする請求項1〜6の
何れか1項に記載のコンクリート製品用混和剤組成物。
7. The admixture composition for concrete products according to any one of claims 1 to 6, which is used for producing a concrete product that is compacted by a vibrator.
【請求項8】 重力加速度3G〜60G の遠心力を加えて成
型するコンクリート製品の製造に用いることを特徴とす
る請求項1〜6の何れか1項に記載のコンクリート製品
用混和剤組成物。
8. The admixture composition for concrete products according to any one of claims 1 to 6, which is used for producing a concrete product which is molded by applying a centrifugal force of gravity acceleration of 3 G to 60 G.
【請求項9】 振動機を使用しないで高流動コンクリー
トの状態で充填成型するコンクリート製品の製造に用い
ることを特徴とする請求項1〜6の何れか1項に記載の
コンクリート製品用混和剤組成物。
9. The admixture composition for concrete products according to claim 1, wherein the admixture composition for concrete products is used for producing a concrete product which is filled and molded in a state of high-fluidity concrete without using a vibrator. Stuff.
JP15483994A 1994-07-06 1994-07-06 Admixture composition for concrete products Expired - Lifetime JP3290304B2 (en)

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* Cited by examiner, † Cited by third party
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WO2001021542A1 (en) * 1999-09-21 2001-03-29 Nippon Nsc Limited Cement dispersant
WO2001021541A1 (en) * 1999-09-21 2001-03-29 Nippon Nsc Limited Cement dispersant
JP2001253750A (en) * 2000-03-08 2001-09-18 Kao Corp Concrete composition for centrifugal forming
JP2002003264A (en) * 2000-06-20 2002-01-09 Taiheiyo Cement Corp Hydraulic compound
EP1466930A3 (en) * 2003-04-10 2006-07-19 Nippon Shokubai Co., Ltd. Polycarboxylic acid cement dispersant and method for producing concrete secondary product

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001021542A1 (en) * 1999-09-21 2001-03-29 Nippon Nsc Limited Cement dispersant
WO2001021541A1 (en) * 1999-09-21 2001-03-29 Nippon Nsc Limited Cement dispersant
JP2001253750A (en) * 2000-03-08 2001-09-18 Kao Corp Concrete composition for centrifugal forming
JP4554023B2 (en) * 2000-03-08 2010-09-29 花王株式会社 Concrete composition for centrifugal molding
JP2002003264A (en) * 2000-06-20 2002-01-09 Taiheiyo Cement Corp Hydraulic compound
EP1466930A3 (en) * 2003-04-10 2006-07-19 Nippon Shokubai Co., Ltd. Polycarboxylic acid cement dispersant and method for producing concrete secondary product
US7232873B2 (en) 2003-04-10 2007-06-19 Nippon Shokubai Co., Ltd. Polycarboxylic acid cement dispersant and method for producing concrete secondary product

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