JPH01115445A - Dispersant composition - Google Patents

Dispersant composition

Info

Publication number
JPH01115445A
JPH01115445A JP62269314A JP26931487A JPH01115445A JP H01115445 A JPH01115445 A JP H01115445A JP 62269314 A JP62269314 A JP 62269314A JP 26931487 A JP26931487 A JP 26931487A JP H01115445 A JPH01115445 A JP H01115445A
Authority
JP
Japan
Prior art keywords
styrene
weight
dispersant composition
dispersant
maleic acid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP62269314A
Other languages
Japanese (ja)
Inventor
Jiro Yasumura
安村 二郎
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.)
Idemitsu Petrochemical Co Ltd
Original Assignee
Idemitsu Petrochemical Co Ltd
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 Idemitsu Petrochemical Co Ltd filed Critical Idemitsu Petrochemical Co Ltd
Priority to JP62269314A priority Critical patent/JPH01115445A/en
Publication of JPH01115445A publication Critical patent/JPH01115445A/en
Pending legal-status Critical Current

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  • Curing Cements, Concrete, And Artificial Stone (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)

Abstract

PURPOSE:To prepare the title dispersant composition useful as various dispersants by adding formalin to the sulfonation product of the mixture of naphthalene and a styrene-maleic acid copolymer to condense the materials, and then neutralizing the condensate. CONSTITUTION:Naphthalene and a styrene-maleic acid copolymer are mixed, and the mixture is sulfonated. In this case, 100pts.wt. naphthalene is ordinarily mixed with 1-500pts.wt. styrene-maleic acid copolymer. Sulfonation is appropriately carried out at 150-180 deg.C and 0-5kg/cm<2>G pressure for 0.5-5hr. Formalin is added to the sulfonation product, and the materials are condensed to produce a dispersant composition. Condensation is appropriately carried out by adding 50-300pts.wt. water and 50-80pts.wt. formalin to 100pts.wt. sulfonation product.

Description

【発明の詳細な説明】 C産業上の利用分野] この発明は分散剤組成物に関し、詳しくは石炭スラリー
用分散剤、セメント用分散剤(セメントベート、モルタ
ルまたはコンクリート用分散剤)、染料用分散剤、顔料
用分散剤、乳化重合用分散剤またはスラッジ用分散剤等
として有用で、しかも効率的な方法で調製された分散剤
組成物に関するものである。
[Detailed Description of the Invention] C. Industrial Field of Application] This invention relates to a dispersant composition, specifically a dispersant for coal slurry, a dispersant for cement (cement bait, mortar or concrete dispersant), and a dispersant for dyes. The present invention relates to a dispersant composition useful as a dispersant for pigments, a dispersant for emulsion polymerization, a dispersant for sludge, etc., and prepared by an efficient method.

[従来の技術] 無機固体粒子や有機微細物質を特定の媒体に分散せしめ
ることは、各種の分野で要求される。そして、通常はそ
の分散性を向上させるために分散剤が用いられる。
[Prior Art] Dispersing inorganic solid particles or organic fine substances in a specific medium is required in various fields. A dispersant is usually used to improve the dispersibility.

たとえば、モルタルやコンクリートにおけるセメント粒
子の水に対する分散性を向上させる分散剤として、ナフ
タレンスルホン酸のホルマリン縮金物の塩およびスルホ
ン化スチレン−マレイン酸共重合体の塩が知られている
(特開昭61−83662号公報)。
For example, salts of formalin condensates of naphthalene sulfonic acid and salts of sulfonated styrene-maleic acid copolymers are known as dispersants that improve the dispersibility of cement particles in water in mortar and concrete (Japanese Patent Application Laid-open No. 61-83662).

これら分散剤はそれぞれ単独で用いられることもあるが
、多くの場合は二者を配合して用いられる。ところが、
従来はこの配合して得られる分散剤組成物を調製するに
あたっては、ナフタリンスルホン酸のホルマリン縮金物
の塩と、スルホン化スチレン−マレイン酸共重合体の塩
をそれぞれ別途に製造し配合していI;。
These dispersants may be used alone, but in most cases, they are used in combination. However,
Conventionally, in preparing the dispersant composition obtained by this blending, a salt of a formalin condensate of naphthalene sulfonic acid and a salt of a sulfonated styrene-maleic acid copolymer were separately manufactured and blended. ;.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

この発明は、従来の二者をそれぞれ別途に製造し配合す
るという煩雑さを解消して、より効率的な方法で調製さ
れてなる分散剤組成物を提供することを目的とする。
An object of the present invention is to provide a dispersant composition prepared by a more efficient method by eliminating the conventional complexity of separately manufacturing and blending the two components.

[問題を解決するための手段] 発明者は、前記の目的を達成するために種々検討を重ね
た結果、当初からす7タレンとスチレン−マレイン酸共
重合体を混合し、この混合物を反応処理することによっ
て、−挙に分散剤組成物が調製できることを見い出し、
この知見に基づいてこの発明をなすに至った。
[Means for Solving the Problem] As a result of various studies to achieve the above object, the inventor initially mixed glass 7-talene and styrene-maleic acid copolymer, and subjected this mixture to a reaction treatment. It has been found that a dispersant composition can be prepared by -
This invention was made based on this knowledge.

すなわち、この発明によれば、ナフタレンとスチレン−
マレイン酸共重合体との混合物をスルホン化し、このス
ルホン化生成物にホルマリンを加えて縮合し、次いで中
和処理してなる分散剤組成物が提供される。
That is, according to this invention, naphthalene and styrene
A dispersant composition is provided by sulfonating a mixture with a maleic acid copolymer, adding formalin to the sulfonated product for condensation, and then neutralizing the mixture.

この発明においては、まず、ナフタレンとスチレン−マ
レイン酸共重合体を混合し、この混合物をスルホン化す
る。両者の混合割合には特別の制限はないが、通常はナ
フタレン100重量部に対して、スチレン−マレイン酸
共重合体を1〜500重量部、好ましくは10〜100
重量部とする。
In this invention, first, naphthalene and a styrene-maleic acid copolymer are mixed, and this mixture is sulfonated. There is no particular restriction on the mixing ratio of both, but usually 1 to 500 parts by weight, preferably 10 to 100 parts by weight of styrene-maleic acid copolymer per 100 parts by weight of naphthalene.
Part by weight.

用いるスチレン−マレイン酸共重合体にも特に制限はな
いが、通常は数平均分子量500〜2ONO1好ましく
は800〜10000のもの、スチレン単位が構成する
割合が20〜90モル%、好ましくは40〜80モル%
のものが望ましい。
There are no particular restrictions on the styrene-maleic acid copolymer used, but it usually has a number average molecular weight of 500 to 2 ONO1, preferably 800 to 10,000, and the proportion of styrene units is 20 to 90 mol%, preferably 40 to 80. mole%
Preferably.

この混合物をスルホン化するにあたっては、通常は溶媒
を用いることなく、スルホン化剤を添加して行う。スル
ホン化剤としては、硫酸、クロル硫酸、発煙硫酸、無水
硫酸等の一般に用いられるスルホン化剤を使用する。こ
のスルホン化剤はす7グレン100重量部に対し、50
〜500重量部、好ましくは70〜200重量部使用す
る。スルホン化剤は一挙に添加してよいし、分割添加し
てもよい。
Sulfonation of this mixture is usually carried out by adding a sulfonating agent without using a solvent. As the sulfonating agent, commonly used sulfonating agents such as sulfuric acid, chlorosulfuric acid, fuming sulfuric acid, and sulfuric anhydride are used. This sulfonating agent is 50 parts by weight per 100 parts by weight of 7 grains.
~500 parts by weight, preferably 70-200 parts by weight are used. The sulfonating agent may be added all at once or may be added in portions.

スルホン化の条件に制限はないが、通常は80〜200
℃、好ましくは150〜180°Cの温度、0−10 
kg/ cra”G 1好ましくはO−5ky/ cm
”Gの圧力で、0.1−10時間、好ましくは0.5〜
5時間反応させれば充分である。
There are no restrictions on the conditions for sulfonation, but usually 80 to 200
°C, preferably 150-180 °C temperature, 0-10
kg/cra”G 1 preferably O-5ky/cm
” at a pressure of 0.1-10 hours, preferably 0.5-10 hours.
A reaction time of 5 hours is sufficient.

この発明においては、ついでこのようにして得られたス
ルホン化生成物にホルマリンを加えて縮合する。
In this invention, formalin is then added to the sulfonated product thus obtained for condensation.

縮合にあたっては、前記スルホン化生成物100重量部
に対し、水2o〜SOO重量部、好ましくは50〜30
0重量部を加え、所望により濃硫酸を0〜100重量部
、好ましくは10〜60重量部添加し、これにホルマリ
ン30〜100重量部、好ましくは50〜80重量部加
えて行う。
In the condensation, 20 to 30 parts by weight of water, preferably 50 to 30 parts by weight, are added to 100 parts by weight of the sulfonated product.
If desired, 0 to 100 parts by weight, preferably 10 to 60 parts by weight of concentrated sulfuric acid are added, and 30 to 100 parts by weight, preferably 50 to 80 parts by weight of formalin are added thereto.

縮合の条件に特別な制限はないが゛、通常は60〜15
0℃、好ましくは80−130’Oの温度、0〜10 
kg/ cm2G、好ましくは0〜5 kg/ cm”
Gノ圧力テ、0.5〜20時間、好ましくは1〜5時間
行う。
There are no special restrictions on the condensation conditions, but usually 60 to 15
Temperature of 0°C, preferably 80-130'O, 0-10
kg/cm2G, preferably 0-5 kg/cm”
G pressure is carried out for 0.5 to 20 hours, preferably for 1 to 5 hours.

この発明においては、このようにして得られた縮合生成
物を中和処理して、目的物である分散剤組成物を得る。
In this invention, the condensation product thus obtained is neutralized to obtain the desired dispersant composition.

中和処理剤としてはナトリウム、カリウム、カルシウム
等の水酸化物、炭酸塩、重炭酸塩、アンモニア、アミン
などを用いることができる。
As the neutralizing agent, hydroxides of sodium, potassium, calcium, etc., carbonates, bicarbonates, ammonia, amines, etc. can be used.

中和処理の条件としても特別な制限はないが、通常は3
0〜100’c、好ましくは50〜80’0で0.5〜
5時間、好ましくは1〜3時間処理すれば足りる。
There are no special restrictions on the conditions for neutralization, but usually 3
0-100'c, preferably 50-80'0 and 0.5-
A treatment time of 5 hours, preferably 1 to 3 hours is sufficient.

[発明の効果] この発明によれば、きわめて効率的に分散剤組成物が調
製され、得られた分散剤組成物は石炭スラリー用分散剤
、セメント用分散剤、染料用分散剤、顔料用分散剤、乳
化重合用分散剤、スラッジ用分散剤等として各種広範な
分散剤として有効に使用することができる。
[Effect of the invention] According to the present invention, a dispersant composition is prepared very efficiently, and the obtained dispersant composition can be used as a dispersant for coal slurry, a dispersant for cement, a dispersant for dyes, and a dispersant for pigments. It can be effectively used as a wide variety of dispersants, such as emulsion polymerization dispersants, sludge dispersants, etc.

[実施例] 次に実施例および使用例をあげて、この発明をさらに詳
細に説明する。
[Example] Next, the present invention will be explained in more detail by giving examples and usage examples.

実施例 す7グレン100gとスチレン−マレイン酸共重合体C
ARCOchemica1社製、S M A −200
0゜数平均分子量1700、酸価37011sIKOH
/ 9) 309を混合し、この混合物を90’Oまで
昇温した後、スルホン化剤として濃硫酸1209を加え
、ついで温度165℃、常圧で2時間反応させてスルホ
ン化を行った。
Example 7 100g of grain and styrene-maleic acid copolymer C
Manufactured by ARCOchemica1, SMA-200
0゜number average molecular weight 1700, acid value 37011sIKOH
/ 9) After mixing 309 and raising the temperature of this mixture to 90'O, concentrated sulfuric acid 1209 was added as a sulfonating agent, and the mixture was then reacted at a temperature of 165° C. and normal pressure for 2 hours to perform sulfonation.

次いでこのスルホン化生成物に水60g、濃硫酸40y
を加え、さらに37重量%のホルマリン609を加えて
、95℃、常圧で4時間反応させて縮合を行った。
Next, 60 g of water and 40 y of concentrated sulfuric acid were added to the sulfonated product.
was added, and further 37% by weight of formalin 609 was added, and the mixture was reacted at 95° C. and normal pressure for 4 hours to perform condensation.

おわりに、こうして得た縮合生成物に、水酸化カルシウ
ム90gを含む乳化液を加え、生成した硫酸カルシウム
をろ過除去し、得られたろ液に30重量%の水酸化ナト
リウム水溶液130gを加え、温度60℃で2.、#間
、中和処理を行い、35重量%水溶液として分散剤組成
物650gを得た。
Finally, an emulsion containing 90 g of calcium hydroxide was added to the condensation product obtained in this way, the produced calcium sulfate was removed by filtration, and 130 g of a 30% by weight aqueous sodium hydroxide solution was added to the obtained filtrate. 2 at °C. , #, neutralization treatment was performed to obtain 650 g of a dispersant composition as a 35% by weight aqueous solution.

使用例1 (石炭スラリーの調製と評価) 第1表に示する石炭(オーストラリア産)2009、実
施例で得た分散剤組成物(35重量%水溶液) 4.6
gおよび水57;を配合した後、モルタ−グラインダに
より湿式粉砕して石炭スラリーを調製した。粉砕された
石炭は、200メツシユ以下の粒径のものが82.5%
であった。
Use example 1 (Preparation and evaluation of coal slurry) Coal (produced in Australia) 2009 shown in Table 1, dispersant composition obtained in Example (35% by weight aqueous solution) 4.6
g and water 57; were mixed, and then wet-pulverized using a mortar grinder to prepare a coal slurry. 82.5% of crushed coal has a particle size of 200 mesh or less.
Met.

第  1  表 この石炭スラリーをビーカーに採り、20°Cにおける
粘度をB型粘度計により測定したところ、990センチ
ポイズであった。
Table 1 This coal slurry was placed in a beaker and its viscosity at 20°C was measured using a B-type viscometer, and found to be 990 centipoise.

また、前記石炭スラリーをプラスチック製容器に採り、
24時間静置した後、16メツシユふるいに通した。
Further, the coal slurry is taken in a plastic container,
After standing for 24 hours, it was passed through a 16-mesh sieve.

容器に残存した石炭スラリーの量と、ふるい上に残存し
た石炭スラリーの量から凝集率を求め、石炭スラリーの
安定性を確認したところ、凝集率は6重量%ときわめて
小さかった。
The agglomeration rate was determined from the amount of coal slurry remaining in the container and the amount of coal slurry remaining on the sieve, and the stability of the coal slurry was confirmed, and the aggregation rate was extremely small at 6% by weight.

凝集率− 使用例2 (コンクリートの調製と評価) セメント(徳山曹達(株)製、普通、ポルトランドセメ
ント)460kg/m”、細骨材(四国大三島長浜産砂
、表乾比重2,52、粗粒率214)673 kg7a
”。
Agglomeration rate - Usage example 2 (Preparation and evaluation of concrete) Cement (manufactured by Tokuyama Soda Co., Ltd., ordinary, Portland cement) 460 kg/m'', fine aggregate (sand from Nagahama, Shikoku University Mishima, surface dry specific gravity 2.52, coarse Particle ratio 214) 673 kg7a
”.

粗骨材(周防花岡産砕石、表乾比g2.’IO1粗粒率
6.48、最大寸法20111111) l114&g
/m’、水161kg/m3および実施例で得た分散剤
組成物(35重量%水溶液) 1.01g量%(セメン
トに対する固形分換算)を強制ミキサーにより撹拌混合
してコンクリートを調製した。
Coarse aggregate (crushed stone from Suohanaoka, surface dry ratio g2.'IO1 coarse grain ratio 6.48, maximum dimension 20111111) l114&g
/m', 161 kg/m3 of water, and 1.01 g amount % (solid content based on cement) of the dispersant composition obtained in the example (35% by weight aqueous solution) were stirred and mixed using a forced mixer to prepare concrete.

このコンクリートの空気量、スランプ値および硬化後の
圧縮強度を測定した。
The air content, slump value, and compressive strength after curing of this concrete were measured.

結果を第2表に示す。The results are shown in Table 2.

第  2  表 *’ JISA−1128 *” JISA−1101 *3JISA−1108 使用例3 (無機顔料スラリーの調製と評価) 重質炭酸カルシウム(日東粉化成工業(株)製、MS−
Zoo)70g、水30gおよび実施例で得t;分散剤
組成物(35重量%水溶液)0.2重量%(重質炭酸カ
ルシウムに対する固形分換算)を容器に採り、20°C
で1分間撹拌混合した後、B型粘度計により粘度を測定
したところ、20°Cにおける粘度は120センチボイ
ズと低いものであっIこ 。
Table 2 *' JISA-1128 *'' JISA-1101 *3 JISA-1108 Usage Example 3 (Preparation and evaluation of inorganic pigment slurry) Heavy calcium carbonate (manufactured by Nitto Kofun Kasei Kogyo Co., Ltd., MS-
Zoo), 30 g of water, and 0.2% by weight (solid content based on heavy calcium carbonate) of the dispersant composition (35% by weight aqueous solution) obtained in the example were placed in a container and heated at 20°C.
After stirring and mixing for 1 minute at 20°C, the viscosity was measured using a B-type viscometer, and the viscosity at 20°C was as low as 120 centivoise.

Claims (1)

【特許請求の範囲】[Claims]  ナフタレンとスチレン−マレイン酸共重合体との混合
物をスルホン化し、このスルホン化生成物にホルマリン
を加えて縮合し、次いで中和処理してなる分散剤組成物
A dispersant composition obtained by sulfonating a mixture of naphthalene and a styrene-maleic acid copolymer, adding formalin to the sulfonated product for condensation, and then neutralizing the mixture.
JP62269314A 1987-10-27 1987-10-27 Dispersant composition Pending JPH01115445A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62269314A JPH01115445A (en) 1987-10-27 1987-10-27 Dispersant composition

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62269314A JPH01115445A (en) 1987-10-27 1987-10-27 Dispersant composition

Publications (1)

Publication Number Publication Date
JPH01115445A true JPH01115445A (en) 1989-05-08

Family

ID=17470619

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62269314A Pending JPH01115445A (en) 1987-10-27 1987-10-27 Dispersant composition

Country Status (1)

Country Link
JP (1) JPH01115445A (en)

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