JP2000169206A - Powdery cement dispersant and its production and cement mixture - Google Patents

Powdery cement dispersant and its production and cement mixture

Info

Publication number
JP2000169206A
JP2000169206A JP10339215A JP33921598A JP2000169206A JP 2000169206 A JP2000169206 A JP 2000169206A JP 10339215 A JP10339215 A JP 10339215A JP 33921598 A JP33921598 A JP 33921598A JP 2000169206 A JP2000169206 A JP 2000169206A
Authority
JP
Japan
Prior art keywords
mixture
cement
powdery
dispersant
formula
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
JP10339215A
Other languages
Japanese (ja)
Other versions
JP4159678B2 (en
Inventor
Hirotaka Isomura
弘隆 磯村
Hiroshi Hayashi
浩志 林
Kazuhisa Tsukada
和久 塚田
Koichi Soeda
孝一 副田
Kenjiro Makino
賢次郎 牧野
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.)
Taiheiyo Cement Corp
Original Assignee
Taiheiyo Cement 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 Taiheiyo Cement Corp filed Critical Taiheiyo Cement Corp
Priority to JP33921598A priority Critical patent/JP4159678B2/en
Priority to PCT/JP1999/006648 priority patent/WO2000032534A1/en
Priority to US09/600,858 priority patent/US6437027B1/en
Priority to EP99973010A priority patent/EP1052232A4/en
Priority to KR1020007007720A priority patent/KR20010034109A/en
Priority to CA002318090A priority patent/CA2318090A1/en
Publication of JP2000169206A publication Critical patent/JP2000169206A/en
Application granted granted Critical
Publication of JP4159678B2 publication Critical patent/JP4159678B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To obtain a dispersant suitable for producing highly fluid cement compositions by adjusting a dispersion consisting mainly of an acrylate- or methacrylate-based polymeric compound to a specific pH followed by adding a reducing agent to the dispersion and then evaporating the resultant dispersion to dryness. SOLUTION: This powdery cement dispersant is obtained by the following process: first a mixture is prepared so as to comprise, as the main component, a polymeric compound, i.e., an acrylate- or methacrylate-based one essentially having respective constitutive units of formula I and formula II (R1 to R3 are each H or methyl; R4 is a 1-3C alkyl; M is H, an alkali metal, alkaline earth metal, ammonium or an organic amine; Y is CH2O or COO; n is 20-109), pref. a polymeric compound composed of 40-80 mol% of the unit of formula I and 1-45 mol% of the unit of formula II, and water or a solvent, the mixture is adjusted to pH 7-9 and then incorporated with a reducing agent to deactivate the oxidative power of the radical reaction initiator left in the mixture; subsequently the resultant mixture is evaporated to dryness and then pulverized.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は流動性に優れたセメ
ント組成物を製造するのに適した粉末状セメント分散剤
の製造方法及びこの製造方法で製造された粉末状セメン
ト分散剤並びにこれを含むセメント混合物に関するもの
で、より詳しくはプレミックス製品などにも予め配合す
ることができるセメント分散剤及びその製造方法に関す
る。
TECHNICAL FIELD The present invention relates to a method for producing a powdery cement dispersant suitable for producing a cement composition having excellent fluidity, a powdery cement dispersant produced by this production method, and a method for producing the same. The present invention relates to a cement mixture, and more particularly, to a cement dispersant which can be preliminarily incorporated into a premix product or the like, and a method for producing the same.

【0002】[0002]

【従来の技術】コンクリートやモルタルなどのセメント
を使用した組成物の強度や耐久性は、一般的に水−セメ
ント比(W/C)を小さくするほど向上する。しかるに
水−セメント比が小さいと流動性や作業性が低下する。
水−セメント比(W/C)が小さくても高い流動性を確
保するためにはセメント分散剤が使用されている。この
ようなセメント分散剤としてはアクリル酸又はメタアク
リル酸などのポリカルボン酸系の高分子化合物を分散有
効成分とする分散剤が広く使用されており、他にナフタ
レンスルホン酸塩ホルマリン縮合物を始めとする幾種か
のスルホン酸塩系のホルマリン縮合物を分散有効成分と
するセメント分散剤も知られている。
2. Description of the Related Art The strength and durability of a composition using a cement such as concrete or mortar generally improve as the water-cement ratio (W / C) decreases. However, when the water-cement ratio is small, the fluidity and workability decrease.
Cement dispersants are used to ensure high fluidity even when the water-cement ratio (W / C) is small. As such a cement dispersant, a dispersant containing a polycarboxylic acid-based polymer compound such as acrylic acid or methacrylic acid as an active ingredient is widely used, and other examples include a naphthalene sulfonate formalin condensate. There are also known cement dispersants containing various kinds of sulfonate-based formalin condensates as active ingredients for dispersion.

【0003】[0003]

【発明が解決しようとする課題】しかしながら、ポリカ
ルボン酸系高分子化合物を主成分とする分散剤は、液状
のものが一般的であり、このため例えば左官材料などで
頻繁に使われるプレミックス製品に予め配合しておくこ
とが実質不可能であったり、粉末状分散剤と比べて輸送
面や容器及び容器処理などで多くの配慮を必要とし、そ
のための経費も割高となること。また、スルホン酸塩系
ホルマリン縮合物ではホルマリンが有害物質であるた
め、その取り扱いや使用に於いて必然的に制約せざるを
得なかった。
However, the dispersant containing a polycarboxylic acid-based polymer compound as a main component is generally in a liquid state, and therefore, for example, a premix product frequently used in plastering materials and the like. It is practically impossible to pre-mix it in advance, or it requires a lot of care in terms of transportation, containers and container treatment as compared with a powdered dispersant, and the cost for that is also expensive. Further, since formalin is a harmful substance in the sulfonate-based formalin condensate, handling and use thereof have necessarily been restricted.

【0004】このためポリカルボン酸系高分子化合物を
主成分とするセメント分散剤を粉末化することも試みら
れているが、一般的にポリカルボン酸系高分子化合物
は、水又は水溶性溶媒中でポリカルボン酸の各単量体と
重合開始剤を原料とする重合反応によって製造される液
状物である。この液状物から既知のセメント混和剤の粉
末化技術(例えば、特公平7−14829号や特許第2
669761号)で水への溶解度が高い粉末状分散剤を
得ようとすると、粉末製造過程中に不溶性のゲルが生成
したり、固結や成分変質することがあって、得られた粉
末は分散作用を始めとする性状面での安定性を欠き易
く、また製造収率も低くなりがちであった。即ち、メタ
アクリレート系又はアクリレート系ポリマーのようなポ
リカルボン酸系高分子化合物を、固形粉末化の為の乾燥
操作を行い易くするため、高濃度で生成させる反応系で
は粘性が高くなり、原料モノマーの重合反応を起すラジ
カル反応開始剤が十分拡散せず反応の不均一化が起こり
易い。このような場合や反応効率を増進するためにラジ
カル反応開始剤を過多に用いた場合などでは、ラジカル
反応開始剤が残存し易く、その場合、濃縮、混練、乾燥
といった粉末化諸工程で生成した所望のポリマーが再重
合を起こして不溶性ゲルと化すことがあり、また更には
生成した所望のポリマーが加水分解によって化学変質す
ることもあって、セメント分散剤としての性能が低下し
易かった。
[0004] For this reason, attempts have been made to powder a cement dispersant containing a polycarboxylic acid polymer as a main component, but generally, the polycarboxylic acid polymer is dissolved in water or a water-soluble solvent. Is a liquid product produced by a polymerization reaction using each monomer of polycarboxylic acid and a polymerization initiator as raw materials. A powdering technique of a known cement admixture from this liquid material (for example, Japanese Patent Publication No. Hei 7-14829 and Patent No. 2)
No. 669761), when an attempt is made to obtain a powdery dispersant having a high solubility in water, an insoluble gel may be formed during the powder production process, or caking or component deterioration may occur. It tends to lack stability in properties such as action, and the production yield tends to be low. That is, in order to easily perform a drying operation for forming a polycarboxylic acid-based polymer compound such as a methacrylate-based or acrylate-based polymer into a solid powder, the viscosity increases in a reaction system in which a high concentration is generated, and the raw material monomer is increased. The radical reaction initiator that causes the polymerization reaction of the above does not sufficiently diffuse, and the reaction tends to be uneven. In such a case or when the radical reaction initiator is excessively used to enhance the reaction efficiency, the radical reaction initiator is likely to remain, and in that case, the radical reaction initiator is formed in various powdering steps such as concentration, kneading, and drying. In some cases, the desired polymer was re-polymerized to form an insoluble gel, and furthermore, the produced desired polymer was chemically deteriorated by hydrolysis, so that the performance as a cement dispersant was liable to decrease.

【0005】[0005]

【課題を解決するための手段】本発明者等は、アクリレ
ート系又はメタアクリレート系高分子化合物を主成分と
する液状分散剤を粉末化するには、液状分散剤を特定の
水素イオン濃度にすることによって粉末化工程でのポリ
カルボン酸系高分子化合物の加水分解を防ぐことがで
き、その結果該高分子化合物の変質並びにこれに伴う性
状低下が抑えられ、また還元剤を添加することで残存ラ
ジカル反応開始剤を失活でき、ゲル化を起こすことなく
単粒化した粉末が容易に得られること。更に、この粉末
をセメントに配合した際の分散作用は従来の液状分散剤
に勝るとも劣らない性状であること等の知見を得、本発
明を完成するに至った。
In order to powder a liquid dispersant containing an acrylate or methacrylate polymer as a main component, the present inventors have set the liquid dispersant to a specific hydrogen ion concentration. This can prevent the hydrolysis of the polycarboxylic acid-based polymer compound in the powdering step, thereby suppressing the deterioration of the polymer compound and the accompanying deterioration in properties, and the residual by adding a reducing agent. A single-grained powder can be easily obtained without deactivating the radical reaction initiator and causing gelation. Further, the present inventors have found that the dispersing action when this powder is blended with cement is not inferior to that of a conventional liquid dispersant, and has completed the present invention.

【0006】即ち、本発明は、次の(1)〜(3)で表
される粉末状セメント分散剤の製造方法、及び(4)で
表される粉末状セメント分散剤、並びに(5)で表され
るセメント混合物である。
That is, the present invention provides a method for producing a powdery cement dispersant represented by the following (1) to (3), a powdery cement dispersant represented by (4), and (5) It is a cement mixture represented.

【0007】(1)分子内に少なくとも下記式(I)及
び(II)
(1) At least one of the following formulas (I) and (II)

【0008】[0008]

【化2】 Embedded image

【0009】(式中、R1、R2及びR3は同一又は異な
って水素原子又はメチル基を示し、R4は炭素数1〜3
のアルキル基を示し、Mは水素原子、アルカリ金属、ア
ルカリ土類金属、アンモニウム又は有機アミンを示し、
Yは−CH2O−又は−COO−を示し、nは20〜1
09を示す。)で表される構成単位を有するアクリレー
ト系若しくはメタアクリレート系高分子化合物を主成分
とし、水又は溶媒を含む混合物に、還元剤を添加し、次
いで乾燥することを特徴とする粉末状セメント分散剤の
製造方法。(2)混合物のpHを7〜9に調整すること
を特徴とする前記(1)の粉末状セメント分散剤の製造
方法。(3)還元剤が易溶性のラジカル反応停止剤であ
ることを特徴とする前記(1)又は(2)の粉末状セメ
ント分散剤の製造方法。(4)前記(1)〜(3)の何
れかの製造方法で製造された粉末状セメント分散剤。
(5)前記(4)の粉末状セメント分散剤とセメントを
含む粉粒又は粉末状のセメント混合物。
Wherein R 1 , R 2 and R 3 are the same or different and each represent a hydrogen atom or a methyl group, and R 4 has 1 to 3 carbon atoms.
And M represents a hydrogen atom, an alkali metal, an alkaline earth metal, ammonium or an organic amine;
Y represents a -CH 2 O-or -COO-, n is 20 to 1
09 is shown. A powdery cement dispersant characterized by comprising adding a reducing agent to a mixture containing acrylate or methacrylate polymer having a structural unit represented by formula (1) as a main component, water or a solvent, and then drying the mixture. Manufacturing method. (2) The method for producing a powdery cement dispersant according to the above (1), wherein the pH of the mixture is adjusted to 7 to 9. (3) The method for producing a powdery cement dispersant according to the above (1) or (2), wherein the reducing agent is a readily soluble radical reaction terminator. (4) A powdery cement dispersant produced by the production method according to any one of (1) to (3).
(5) A powdery granule or a powdery cement mixture containing the powdery cement dispersant of the above (4) and cement.

【0010】[0010]

【発明の実施の形態】本発明の粉末状セメント分散剤
は、分子内に少なくとも前記式(I)及び(II)の構
成単位を有するメタアクリレート系若しくはアクリレー
ト系(以下(メタ)アクリレート系と称す)の高分子化
合物を主成分とするものである。該高分子化合物の製造
は、水又は溶媒中で所望の単量体を共重合させる公知技
術であれば特に限定されないが、最も一般的な製造例を
挙げるなら、水又は低級アルコールなどの水溶性有機溶
媒中で、前記式(I)を有する(メタ)アクリレートモ
ノマーと前記式(II)を有する(メタ)アクリレート
系モノマーに、重合開始剤として共重合反応温度以下で
分解しラジカルを発生する公知の易溶性ラジカル反応開
始剤、例えば過硫酸カリウム、過硫酸アンモニウム等の
過硫酸塩や過酸化水素などの過酸化物で代表される無機
系酸化剤若しくは2,2’−アゾビス(2−アミジノプ
ロパン)二塩酸塩などの有機系酸化剤などを加えて共重
合反応せしめることにより得られるものである。
BEST MODE FOR CARRYING OUT THE INVENTION The powdery cement dispersant of the present invention has a methacrylate or acrylate (hereinafter referred to as (meth) acrylate) having at least the structural units of the formulas (I) and (II) in the molecule. )) As a main component. The production of the polymer compound is not particularly limited as long as it is a known technique of copolymerizing a desired monomer in water or a solvent, but the most common production example is water-soluble such as water or a lower alcohol. In an organic solvent, a (meth) acrylate monomer having the formula (I) and a (meth) acrylate monomer having the formula (II) are decomposed as a polymerization initiator at a temperature lower than a copolymerization reaction temperature to generate radicals. An inorganic oxidizing agent represented by persulfates such as potassium persulfate and ammonium persulfate and peroxides such as hydrogen peroxide or 2,2'-azobis (2-amidinopropane) It is obtained by adding an organic oxidizing agent such as dihydrochloride and causing a copolymerization reaction.

【0011】本発明の粉末状セメント分散剤の主成分た
る(メタ)アクリレート系高分子化合物中の各構成単位
の構成量は、前記(I)式で表される構成単位が40〜
80モル%であることが好ましく、より好ましくは45
〜75モル%であり、(II)式で表される構成単位は
1〜45モル%が好ましく、より好ましくは3〜40モ
ル%のものである。式(I)の中のMは、水素原子、ア
ルカリ金属、アルカリ土類金属、アンモニウム又はエタ
ノールアミン等のアルカノールアミン等が挙げられる。
また、式(II)中のnは、20〜109の数を表すが
nが20未満であると、大気中での化学的安定性が劣化
し、またnが109を超えると分散能力が低下するため
何れも好ましくない。R4で示されるアルキル基として
は、メチル基、エチル基、n−プロピル基、i−プロピ
ル基が挙げられる。
The constituent amount of each constituent unit in the (meth) acrylate polymer compound which is the main component of the powdery cement dispersant of the present invention is such that the constituent unit represented by the above formula (I) is 40 to 40%.
It is preferably 80 mol%, more preferably 45 mol%.
The content of the structural unit represented by the formula (II) is preferably from 1 to 45 mol%, more preferably from 3 to 40 mol%. M in the formula (I) includes a hydrogen atom, an alkali metal, an alkaline earth metal, ammonium or an alkanolamine such as ethanolamine.
Further, n in the formula (II) represents a number of 20 to 109, and when n is less than 20, chemical stability in the air is deteriorated, and when n exceeds 109, the dispersion capacity is reduced. Are not preferred. The alkyl group represented by R 4, a methyl group, an ethyl group, n- propyl group, i- propyl group.

【0012】構成単位(II)は、Yが−CH2O−の
ものと−COO−のものの2種類あるが、何れか一方の
みの存在でも両方が存在するものであっても良い。両方
存在の場合は、何れか一方の構成単位の平均分子数nが
20〜109の範囲であれば良く、その存在量はYが−
COO−である(II)が1〜30モル%であってYが
−CH2O−である(II)が1〜30モル%であるも
のが好ましい。
In the structural unit (II), there are two types of units, in which Y is —CH 2 O— or —COO—, but it is also possible for only one or both to be present. When both are present, the average molecular number n of one of the constituent units may be in the range of 20 to 109, and the abundance of Y is-
A is (II) is preferably one comprising from 1 to 30 mol%, Y is -CH 2 O-(II) is 1 to 30 mol% COO-.

【0013】また、本発明に於ける(メタ)アクリレー
ト系高分子化合物は前記式(I)及び(II)で表され
る構成単位を含む他に、下記式(III)又は(IV)
で表される構成単位の1以上を有するものであっても良
い。
The (meth) acrylate polymer compound of the present invention contains not only the structural units represented by the above formulas (I) and (II) but also the following formula (III) or (IV)
May have one or more structural units represented by

【0014】[0014]

【化3】 Embedded image

【0015】(式中、R5は水素原子又はメチル基を示
し、R6は炭素数1〜3のアルキル基を示し、Xは−S
32−又は−O−Ph−SO32を示す。但し、Mは
水素原子、アルカリ金属、アルカリ土類金属、アンモニ
ウム又はアルカノールアミンを示し、Phはフェニレン
基を示す。)
(Wherein, R 5 represents a hydrogen atom or a methyl group, R 6 represents an alkyl group having 1 to 3 carbon atoms, and X represents —S
Showing a or -O-Ph-SO 3 M 2 - O 3 M 2. Here, M represents a hydrogen atom, an alkali metal, an alkaline earth metal, ammonium or an alkanolamine, and Ph represents a phenylene group. )

【0016】構成単位(III)及び(IV)式に於い
て、R6で示される炭素数1〜3のアルキル基として
は、メチル基、エチル基、n−プロピル基、i−プロピ
ル基が挙げられる。(III)式で表される構成単位の
構成量は好ましくは2〜25モル%、より好ましくは5
〜15モル%である。なお、モル%は(I)〜(IV)
の全構成単位の合計を100モル%とした場合の各々の
モル%を示す。
In the structural units (III) and (IV), examples of the alkyl group having 1 to 3 carbon atoms represented by R 6 include a methyl group, an ethyl group, an n-propyl group and an i-propyl group. Can be The constituent amount of the constituent unit represented by the formula (III) is preferably 2 to 25 mol%, more preferably 5 to 25 mol%.
1515 mol%. In addition, mol% is (I)-(IV)
Are shown as mol% when the total of all the structural units is 100 mol%.

【0017】また、(I)〜(IV)式に於いて、R1
〜R6はメチル基が特に好ましく、またMはナトリウム
が、Xは−SO3Naが特に好ましい。本分散剤で主成
分たる(メタ)アクリレート系高分子化合物は望ましく
は(I)〜(IV)式で表される全ての構成単位を含む
ものが良い。また、このような(メタ)アクリレート系
高分子化合物の数平均分子量は、好ましくは2000〜
50000、より好ましくは3500〜30000のも
のである。
In the formulas (I) to (IV), R 1
To R 6 is particularly preferably a methyl group, and M is sodium, X is -SO 3 Na are particularly preferred. The (meth) acrylate-based polymer compound as the main component in the dispersant desirably contains all the structural units represented by the formulas (I) to (IV). Further, the number average molecular weight of such a (meth) acrylate polymer compound is preferably from 2000 to 2000.
50,000, more preferably 3500 to 30000.

【0018】本発明の粉末状セメント分散剤は、このよ
うな(メタ)アクリレート系高分子化合物を主成分とし
て含む液状の混合物を乾燥し、粉末化することにより得
られる。尚、該混合物の残部はその殆どが主成分合成時
に用いられた溶媒と重合反応による副生成物に由来する
ものである。
The powdery cement dispersant of the present invention can be obtained by drying and pulverizing a liquid mixture containing such a (meth) acrylate polymer as a main component. Most of the remainder of the mixture is derived from the solvent used in the synthesis of the main component and by-products of the polymerization reaction.

【0019】次に、この液状混合物を粉末化する方法に
ついて詳しく説明する。前記液状の混合物は通常は酸性
液となっているので、この場合、水酸化ナトリウム、水
酸化カリウム、水酸化カルシウムなどのアルカリ金属又
はアルカリ土類金属の水溶液を加え、pHを7〜9に調
整する。pHを調整するのは後の加温乾燥処理時に混合
物中の高分子化合物が加水分解を起こし易く、この加水
分解による変質及び性状劣化を防ぐためである。pH7
未満であると還元剤を大量に必要とするので好ましくな
く、またpH9を超えると加水分解を起こし易くなった
り、乾燥時に離脱される水分のCOD値が高くなるので
好ましくない。尚、液状混合物が当初よりpH7〜9で
ある場合はpH調整剤の類を添加して調整する必要はな
い。次いで、pH値が7〜9の混合物に還元剤を添加す
る。還元剤は主成分たる前記高分子化合物と殆ど反応を
生じない公知還元剤であれば良く、望ましくは高分子化
合物の重合に用いたラジカル反応開始剤に応じて選定さ
れるものであって、一例を挙げると、易溶性の過酸化物
を使用した場合には、還元剤に亜硫酸塩、亜硝酸塩、チ
オ硫酸塩を使用するなど、一般に強い酸化力を有するラ
ジカル反応開始剤に対し概ね対局の還元力を有するもの
とする。このような還元剤としては共重合反応を停止す
る際に通常用いられている易溶性のラジカル反応停止剤
が特に好適である。還元剤の添加量は、混合物中に残存
するラジカル反応開始剤の種類や残存量に応じて決定す
れば良く、通常は高分子化合物合成に用いたラジカル反
応開始剤の固形分の量(モル%値)以下で残存ラジカル
反応開始剤の酸化力を失活できる量以上とするのが望ま
しい。
Next, a method of pulverizing the liquid mixture will be described in detail. Since the liquid mixture is usually an acidic solution, the pH is adjusted to 7 to 9 by adding an aqueous solution of an alkali metal or alkaline earth metal such as sodium hydroxide, potassium hydroxide, or calcium hydroxide. I do. The reason for adjusting the pH is to prevent the polymer compound in the mixture from being easily hydrolyzed during the subsequent heating and drying treatment, and to prevent the deterioration and property deterioration due to the hydrolysis. pH 7
If the pH is less than 1, it is not preferable because a large amount of a reducing agent is required, and if the pH is more than 9, hydrolysis is liable to occur, and the COD value of water released during drying is not preferable. When the liquid mixture has a pH of 7 to 9 from the beginning, it is not necessary to adjust the pH by adding a pH adjuster or the like. Subsequently, a reducing agent is added to the mixture having a pH value of 7-9. The reducing agent may be a known reducing agent that hardly reacts with the polymer compound as a main component, and is preferably selected according to a radical reaction initiator used for polymerizing the polymer compound. In general, when a readily soluble peroxide is used, sulfites, nitrites, and thiosulfates are used as reducing agents. Shall have power. As such a reducing agent, a readily soluble radical reaction terminator that is generally used when terminating a copolymerization reaction is particularly preferable. The amount of the reducing agent to be added may be determined according to the type and the remaining amount of the radical reaction initiator remaining in the mixture, and usually, the amount of the solid content (mol%) of the radical reaction initiator used in the synthesis of the polymer compound is used. Value) or less, it is desirable that the amount is not less than an amount that can deactivate the oxidizing power of the residual radical reaction initiator.

【0020】還元剤添加後は混練・攪拌する。混練・攪
拌の温度は、40〜120℃程度が好ましく、より好ま
しくは60〜100℃程度とする。混練・攪拌は大気中
でも行うことができるが、変質防止の観点から減圧下又
は窒素やアルゴンなどの不活性ガス雰囲気中で行うのが
望ましい。混練・攪拌したものは乾燥するが、実質混練
・攪拌中に於ける加温により乾燥が開始される。乾燥は
熱風式などの対流型の乾燥装置又は熱伝導型の乾燥装置
であれば特に限定されないが、処理物が5〜40%の溶
液の場合は前者の乾燥装置であるスプレードライヤー、
フラッシュジェットドライヤーなどが適している。処理
物が40%を越える高濃度溶液や粘弾性の高いものの場
合は、後者の攪拌混練乾燥機型、バンド型連続真空乾燥
機等の乾燥機を挙げることができる。前者を用いる場合
は比較的短時間で大量の乾燥を行うことができ、後者を
使用する場合は混練攪拌を行いながら乾燥を行うことが
できる。このような乾燥操作を行うことにより、粉末状
のセメント分散剤を得ることができる。尚、乾燥後の粉
末は小塊状に凝集している場合もあるが、この塊状物は
脆弱であるため僅かな解砕力で容易に単粒子化できる。
After adding the reducing agent, the mixture is kneaded and stirred. The temperature for kneading and stirring is preferably about 40 to 120 ° C, more preferably about 60 to 100 ° C. The kneading / stirring can be performed in the air, but is preferably performed under reduced pressure or in an atmosphere of an inert gas such as nitrogen or argon from the viewpoint of preventing deterioration. The kneaded and agitated one is dried, but the drying is started by heating substantially during the kneading and agitating. Drying is not particularly limited as long as it is a convection type drying apparatus such as a hot air type or a heat conduction type drying apparatus. However, when the processed product is a 5 to 40% solution, the former drying apparatus, a spray dryer,
Flash jet dryers are suitable. When the processed product is a high-concentration solution exceeding 40% or a material having high viscoelasticity, the latter can be exemplified by a drying machine such as a stirring kneading drying machine type or a band type continuous vacuum drying machine. When the former is used, a large amount of drying can be performed in a relatively short time, and when the latter is used, drying can be performed while kneading and stirring. By performing such a drying operation, a powdery cement dispersant can be obtained. The dried powder may be agglomerated into small agglomerates, but the agglomerates are fragile and can be easily formed into single particles with a slight crushing force.

【0021】粉末化したセメント分散剤は、使用上の利
便性から、任意の粉砕・分級方法により平均粒径5〜2
000μm、より好ましくは10〜500μmに調整す
ることが望ましい。
The powdered cement dispersant may have an average particle size of 5 to 2 by an arbitrary pulverizing / classifying method for convenience in use.
It is desirable to adjust the thickness to 000 μm, more preferably 10 to 500 μm.

【0022】本発明の粉末状セメント分散剤を適用でき
るセメントは特に限定されず、普通ポルトランドセメン
ト、高炉セメント、シリカセメント、フライアッシュセ
メント等の混合セメント、また、超速硬セメント、低ア
ルカリセメントでも良く、また速硬剤を含有させた吹付
け用セメント、更には高炉スラグやフライアッシュ等を
骨材成分として含むコンクリート組成物であっても良
い。本分散剤のセメントへの配合量は、セメント100
重量部に対し、0.01〜5重量部が適値であり、この
中でもセメント100重量部に対し、0.05〜3重量
部の本分散剤を含有せしめた粉粒又は粉末状のセメント
混合物とするのが特に好ましい。尚、本分散剤の添加が
0.01重量部未満の場合は分散効果が乏しくなり、ま
た5重量部を超える添加を行ってもそれ以上分散性が向
上しないので何れも好ましくない。
The cement to which the powdery cement dispersant of the present invention can be applied is not particularly limited, and may be a mixed cement such as ordinary Portland cement, blast furnace cement, silica cement, fly ash cement, ultra-rapid hardening cement, or low alkali cement. Further, a spraying cement containing a quick-hardening agent, or a concrete composition containing blast furnace slag, fly ash, or the like as an aggregate component may be used. The compounding amount of the dispersant in the cement is 100
A suitable value is 0.01 to 5 parts by weight, based on 100 parts by weight of cement, of which 0.05 to 3 parts by weight of the present dispersant is contained in a powder or a cement mixture in powder form. It is particularly preferred that If the amount of the dispersant is less than 0.01 part by weight, the dispersing effect is poor, and if the amount exceeds 5 parts by weight, the dispersibility is not further improved.

【0023】[0023]

【実施例】以下、本発明を実施例により具体的に説明す
る。重合開始剤として(NH4228を用いて製造さ
れ、分子量と構成単位(I)〜(IV)並びにその構成
比(モル%)がそれぞれ表1で表される(A)〜(D)
の(メタ)アクリレート系高分子化合物を主成分とする
固形分濃度が45%でpHが6.7(実施例1と5)又
は6.1(実施例2〜4、6〜9、比較例1〜3)の液
状混合物各800gに、pH調整を行うもの(実施例1
〜9、比較例3)についてはこの溶液に10重量%の水
酸化ナトリウム水溶液75.2gを加え、常温で約3分
間ハンドミキサーにて攪拌を行った後、還元剤を添加
し、これを処理容積が1リットルのニーダー型混練攪拌
機に入れて温度90℃、30torrの減圧下で混練し
ながら濃縮・乾燥を行った。
The present invention will be described below in more detail with reference to examples. It is produced using (NH 4 ) 2 S 2 O 8 as a polymerization initiator, and the molecular weight, the structural units (I) to (IV) and the structural ratio (mol%) are shown in Table 1 (A) to (A). (D)
(Meth) acrylate polymer compound as a main component, the solid content concentration is 45%, and the pH is 6.7 (Examples 1 and 5) or 6.1 (Examples 2 to 4, 6 to 9, Comparative Example) One in which 800 g each of the liquid mixture of 1) to 3) is subjected to pH adjustment (Example 1)
9 to 9 and Comparative Example 3), 75.2 g of a 10% by weight aqueous solution of sodium hydroxide was added to this solution, and the mixture was stirred at room temperature for about 3 minutes with a hand mixer, and then a reducing agent was added. The mixture was placed in a kneader-type kneader-stirring machine having a volume of 1 liter and concentrated and dried while kneading at a temperature of 90 ° C. under a reduced pressure of 30 torr.

【0024】[0024]

【表1】 [Table 1]

【0025】尚、使用した混合物の主成分(高分子化合
物)の種類(表1で示した(A)〜(D)を用いて表
示)、液状混合物のpH値、但しpH調整したものは調
整後のpH値、及び還元剤種とその添加量(混合物の固
形分重量に対する重量%)をそれぞれ表2に表す。ま
た、前記乾燥操作によって得られたものの状態も表2に
記す。
The type of the main component (polymer compound) of the mixture used (indicated by using (A) to (D) shown in Table 1), the pH value of the liquid mixture, and the pH-adjusted one is adjusted. Table 2 below shows the pH value, and the type of reducing agent and the amount added (% by weight based on the weight of the solid content of the mixture). Table 2 also shows the state of the product obtained by the drying operation.

【0026】[0026]

【表2】 [Table 2]

【0027】次に、このようにして得た乾燥粉末を、普
通ポルトランドセメント100g(太平洋セメント
(株)社製)に0.14g加えて乾式混合し、平均粒径
250μmの粉粒状のセメント混合物を作製した。この
セメント混合物に、水30gを加えてホバートミキサー
で3分間混練し、混練物のペーストフロー値を測定し
た。水を加えて混練した際の該乾燥粉末の溶解状態及び
ペーストフロー値(mm)も表2に併せて記す。また、
比較例4として市販品のナフタレンスルホン酸塩ホルマ
リン縮合物を主成分とする液状のセメント分散剤、比較
例5として市販品のポリカルボン酸系高分子化合物を主
成分とする液状のセメント分散剤、比較例6として市販
品のポリカルボン酸系高分子化合物を主成分とする粉末
状のセメント分散剤を用い、それぞれ固形分重量換算で
0.88gをセメント100gと水30gに添加混練し
て得たペーストのフロー値も測定した。尚、ペーストフ
ロー値の測定は、水平に設置した磨き板ガラス上に、内
径50mm、高さ51mmの硬質樹脂製円筒状パイプ
(内容積100ml)を垂直に置き、混練したセメント
ペーストをこのパイプ上端まで充填した後、直ぐにパイ
プを引き上げ、流れたペーストの広がりが止った後、こ
の広がりの直交する任意の2方向の直径を測定し、その
平均値をペーストフロー値とした。
Next, 0.14 g of the dry powder thus obtained was added to 100 g of ordinary Portland cement (manufactured by Taiheiyo Cement Co., Ltd.) and dry-mixed to obtain a powdery cement mixture having an average particle size of 250 μm. Produced. 30 g of water was added to this cement mixture and kneaded for 3 minutes with a Hobart mixer, and the paste flow value of the kneaded product was measured. Table 2 also shows the dissolved state of the dried powder and the paste flow value (mm) when water was added and kneaded. Also,
As Comparative Example 4, a liquid cement dispersant mainly containing a commercially available naphthalene sulfonate formalin condensate, as a comparative example 5, a liquid cement dispersant mainly containing a commercially available polycarboxylic acid polymer compound, Comparative Example 6 was obtained by adding and kneading 0.88 g in terms of solids weight to 100 g of cement and 30 g of water using a powdery cement dispersant mainly containing a commercially available polycarboxylic acid polymer compound as a main component. The flow value of the paste was also measured. The paste flow value was measured by placing a hard resin cylindrical pipe (with an inner volume of 100 ml) having an inner diameter of 50 mm and a height of 51 mm vertically on a horizontally polished glass plate, and kneading the cement paste to the top of the pipe. Immediately after filling, the pipe was pulled up, and after the spread of the flowing paste stopped, the diameters in any two directions perpendicular to the spread were measured, and the average value was defined as the paste flow value.

【0028】[0028]

【発明の効果】本発明の粉末状セメント分散剤の製造方
法は、比較的簡単な工程と手法で行うことができ、従来
見られた品質性能や製造収率の低下を十分改善すること
ができる。本法で製造された粉末状セメント分散剤は、
液状のセメント分散剤と比較し、少ない使用量で勝ると
も劣らない優れた分散性状を発現することができる。ま
た、本分散剤は、予めセメント等に加えて粉粒状の混合
物として保管・輸送することもできるため、いわゆるプ
レミックス製品などに利用できる。
The method for producing a powdery cement dispersant of the present invention can be carried out by relatively simple steps and techniques, and can sufficiently improve the reduction in quality performance and production yield that has been seen in the past. . The powdery cement dispersant manufactured by this method is
As compared with a liquid cement dispersant, excellent dispersibility can be achieved with a small amount of use. In addition, since the present dispersant can be stored and transported as a powdery mixture in addition to cement or the like in advance, it can be used for so-called premix products.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C04B 103:40 111:00 (72)発明者 副田 孝一 千葉県佐倉市大作二丁目4番2号 太平洋 セメント株式会社佐倉研究所内 (72)発明者 牧野 賢次郎 宮崎県延岡市桜ヶ丘二丁目517番57号 Fターム(参考) 4G012 MC00 PA01 PB31 PC01 4J002 BG011 BG071 BQ001 CH051 DF036 DG046 EE016 FD206 GL00 HA09 ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) C04B 103: 40 111: 00 (72) Inventor Koichi Soeda 2-4-2 Daisaku, Sakura City, Chiba Pref. Pacific Cement Inside Sakura Laboratory Co., Ltd. (72) Inventor Kenjiro Makino 2-517 Sakuragaoka, Nobeoka City, Miyazaki Prefecture F-term (reference) 4G012 MC00 PA01 PB31 PC01 4J002 BG011 BG071 BQ001 CH051 DF036 DG046 EE016 FD206 GL00 HA09

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 分子内に少なくとも下記式(I)及び
(II) 【化1】 (式中、R1、R2及びR3は同一又は異なって水素原子
又はメチル基を示し、R4は炭素数1〜3のアルキル基
を示し、Mは水素原子、アルカリ金属、アルカリ土類金
属、アンモニウム又は有機アミンを示し、Yは−CH2
O−又は−COO−を示し、nは20〜109を示
す。)で表される構成単位を有するアクリレート系若し
くはメタアクリレート系高分子化合物を主成分とし、水
又は溶媒を含む混合物に、還元剤を添加し、次いで乾燥
することを特徴とする粉末状セメント分散剤の製造方
法。
1. A compound having at least the following formulas (I) and (II) in a molecule: (Wherein, R 1 , R 2 and R 3 are the same or different and represent a hydrogen atom or a methyl group, R 4 represents an alkyl group having 1 to 3 carbon atoms, M represents a hydrogen atom, an alkali metal, an alkaline earth, metal, shows the ammonium or organic amine, Y is -CH 2
O- or -COO- is shown, and n shows 20-109. A powdery cement dispersant characterized by comprising adding a reducing agent to a mixture containing acrylate or methacrylate polymer having a structural unit represented by formula (1) as a main component, water or a solvent, and then drying the mixture. Manufacturing method.
【請求項2】 混合物のpHを7〜9に調整することを
特徴とする請求項1記載の粉末状セメント分散剤の製造
方法。
2. The method for producing a powdery cement dispersant according to claim 1, wherein the pH of the mixture is adjusted to 7 to 9.
【請求項3】 還元剤が易溶性のラジカル反応停止剤で
あることを特徴とする請求項1又は2記載の粉末状セメ
ント分散剤の製造方法。
3. The method for producing a powdery cement dispersant according to claim 1, wherein the reducing agent is an easily soluble radical reaction terminator.
【請求項4】 前記請求項1〜3の何れかの製造方法で
製造された粉末状セメント分散剤。
4. A powdery cement dispersant produced by the production method according to claim 1.
【請求項5】 前記請求項4の粉末状セメント分散剤と
セメントを含む粉粒又は粉末状のセメント混合物。
5. A powdery or powdery cement mixture comprising the powdery cement dispersant of claim 4 and cement.
JP33921598A 1998-11-30 1998-11-30 Powdered cement dispersant, method for producing the same, and cement mixture Expired - Lifetime JP4159678B2 (en)

Priority Applications (6)

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JP33921598A JP4159678B2 (en) 1998-11-30 1998-11-30 Powdered cement dispersant, method for producing the same, and cement mixture
PCT/JP1999/006648 WO2000032534A1 (en) 1998-11-30 1999-11-29 Process for producing dispersant for powdery hydraulic composition
US09/600,858 US6437027B1 (en) 1998-11-30 1999-11-29 Process for producing dispersant for powdery hydraulic composition
EP99973010A EP1052232A4 (en) 1998-11-30 1999-11-29 Process for producing dispersant for powdery hydraulic composition
KR1020007007720A KR20010034109A (en) 1998-11-30 1999-11-29 Process for producing dispersant for powdery hydraulic composition
CA002318090A CA2318090A1 (en) 1998-11-30 1999-11-29 Process for producing dispersant for powdery hydraulic composition

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002080260A (en) * 2000-06-26 2002-03-19 Taiheiyo Cement Corp Cast-in-place water-permeable concrete and driveway pavement
JP2003002712A (en) * 2001-06-15 2003-01-08 Taiheiyo Cement Corp Producing method of powdery cement dispersing agent
JP2016515505A (en) * 2013-03-26 2016-05-30 ビーエーエスエフ ソシエタス・ヨーロピアBasf Se Rapid suspension powder composition
CN107189026A (en) * 2017-05-15 2017-09-22 安徽森普新型材料发展有限公司 A kind of preparation method of ester ether composite polymeric polycarboxylate water-reducer
JP2017535644A (en) * 2014-11-10 2017-11-30 ビーエーエスエフ ソシエタス・ヨーロピアBasf Se Polymers with polyether side chains
WO2021132317A1 (en) 2019-12-25 2021-07-01 花王株式会社 Method for producing powder dispersant composition for hydraulic composition
JP2022007923A (en) * 2019-12-25 2022-01-13 花王株式会社 Method of producing powder dispersant composition for hydraulic composition

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002080260A (en) * 2000-06-26 2002-03-19 Taiheiyo Cement Corp Cast-in-place water-permeable concrete and driveway pavement
JP4594503B2 (en) * 2000-06-26 2010-12-08 太平洋セメント株式会社 On-site permeable concrete and road pavement
JP2003002712A (en) * 2001-06-15 2003-01-08 Taiheiyo Cement Corp Producing method of powdery cement dispersing agent
JP2016515505A (en) * 2013-03-26 2016-05-30 ビーエーエスエフ ソシエタス・ヨーロピアBasf Se Rapid suspension powder composition
JP2017535644A (en) * 2014-11-10 2017-11-30 ビーエーエスエフ ソシエタス・ヨーロピアBasf Se Polymers with polyether side chains
CN107189026A (en) * 2017-05-15 2017-09-22 安徽森普新型材料发展有限公司 A kind of preparation method of ester ether composite polymeric polycarboxylate water-reducer
WO2021132317A1 (en) 2019-12-25 2021-07-01 花王株式会社 Method for producing powder dispersant composition for hydraulic composition
JP2022007923A (en) * 2019-12-25 2022-01-13 花王株式会社 Method of producing powder dispersant composition for hydraulic composition
JP7286609B2 (en) 2019-12-25 2023-06-05 花王株式会社 Method for producing powder dispersant composition for hydraulic composition

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