JPS5936509A - Composition for defoaming and its production - Google Patents

Composition for defoaming and its production

Info

Publication number
JPS5936509A
JPS5936509A JP14527082A JP14527082A JPS5936509A JP S5936509 A JPS5936509 A JP S5936509A JP 14527082 A JP14527082 A JP 14527082A JP 14527082 A JP14527082 A JP 14527082A JP S5936509 A JPS5936509 A JP S5936509A
Authority
JP
Japan
Prior art keywords
ethylene
stearylamide
type
composition
weight
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
JP14527082A
Other languages
Japanese (ja)
Other versions
JPS646803B2 (en
Inventor
Osamu Umekawa
梅川 治
Kazushige Kaimoto
開本 和繁
Sakae Katayama
片山 榮
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.)
Katayama Chemical Inc
Original Assignee
Katayama Chemical Inc
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 Katayama Chemical Inc filed Critical Katayama Chemical Inc
Priority to JP14527082A priority Critical patent/JPS5936509A/en
Publication of JPS5936509A publication Critical patent/JPS5936509A/en
Publication of JPS646803B2 publication Critical patent/JPS646803B2/ja
Granted legal-status Critical Current

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Abstract

PURPOSE:To provide a compsn. for defoaming having specified defoaming performance by using liquid hydrocarbon oil and ethylene-bis-stearylamide consisting of >=80% beta type. CONSTITUTION:>=80% portion of ethylene-bis-stearylamide used in a titled compsn. has a beta type crystalline form. Either arom. or aliphat. liquid hydrocarbon oil is usable and the oil having 10-40cps (100 deg.F) viscosity is preferred in terms of stability. Paraffin oil is most preferable. The ethylene-bis-stearylamide is suspended in such hydrocarbon oil, and the suspension thereof is heat-treated at about 45-90 deg.C to convert and adjust predominant alpha-type portion of the ethylene-bis-stearylamide in such a way that >=80wt% thereof has a beta type. The compsn. for defoaming is thus obtd. It is preferred to contain 1-10pts.wt. ethylene-bis-stearylamide and 99-90pts.wt. liquid hydrocarbon.

Description

【発明の詳細な説明】 この発明は消泡用組成物に関する。さらに詳しくは、優
れた消泡効果を有する消泡組成物及びその製造法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION This invention relates to antifoaming compositions. More specifically, the present invention relates to an antifoaming composition having an excellent antifoaming effect and a method for producing the same.

従来から、脂肪酸アミドと鉱油とを主成分とする消泡用
組成分が種々提案されており、ことにエチレンビスステ
アリルアミドと鉱油とを主成分トする消泡剤は、パルプ
工業や製紙工業、各種工業廃水等における消泡用途に広
く用いられている。これらの消泡剤は通常、加熱処理や
機械的攪拌等にヨリエチレンビスステアリルアミド又は
それを主体とする混合脂肪酸アミドを鉱油中に均一に懸
濁させ、任意に補助成分を加えることにより得られてい
る。
Various antifoaming compositions containing fatty acid amide and mineral oil as main components have been proposed in the past.In particular, antifoaming agents containing ethylene bisstearylamide and mineral oil as main components are used in the pulp industry, paper manufacturing industry, Widely used for defoaming purposes in various industrial wastewater, etc. These antifoaming agents are usually obtained by uniformly suspending yoriethylenebisstearylamide or a mixed fatty acid amide based on it in mineral oil by heat treatment or mechanical stirring, and optionally adding auxiliary ingredients. ing.

しかしながら、これらの消泡剤は、有効成分を一定の割
合に保っているにも拘らず、消泡性能が必ずしも一定で
ないという問題点があった。
However, these antifoaming agents have a problem in that their antifoaming performance is not necessarily constant even though the active ingredients are kept at a constant ratio.

この発明は、この問題点を解消すべくなされたものであ
る。この発明の発明者らはまず、懸濁されてなるエチレ
ンビスステアリルアミドの結晶形に注目し鋭意研究を行
なった。
This invention was made to solve this problem. The inventors of the present invention first focused on the crystalline form of suspended ethylene bisstearylamide and conducted extensive research.

エチレンビスステアリルアミドは例えば特開昭51−6
8487号公報等に開示された方法、すなわちエチレン
ジアミン1モル当りステアリン酸2モルを反応させるこ
とにより製造され、工業的にはステアリン酸単独ではな
くステアリン酸を主体とする混合脂肪酸と反応して製造
され、通常の消泡剤の用途には後者すなわちエチレンビ
スステアリルアミドを主体とする混合脂肪酸アミドが用
いられている。いずれにせよこのようにして得られたエ
チレンビスステアリルアミドの結晶形uはα型とβ型か
らなり、ことにα型が優位である(米国特許第4248
792号明細書等参照)。そしてα型とβ型とは次に示
すような波数における赤外吸収特性に差異があるので充
分に区別しうるものである3、 波数(備−’)1248 955 940 678α型
   なし  あり なし あり β型   あり  なし あり なし この発明の発明者らは、かような結晶形態の異なりやそ
の構成割合が、消泡性能に何んらかの影響を与えている
のではないかという新たな問題提起を行ない、研究、検
討を重ねた結果、意外にもエチレンビスステアリルアミ
ドの主要な結晶形であるα型とβ型との間で消泡性能に
著しい差があり、β型の方が消泡作用が著しく大きいこ
と、及び消泡用組成物製造時の温度変化によりエチレン
ビスステアリルアミドにおけるα型とβ型との比率が変
化しこれが原因となって消泡性能が変動することを見出
しこの発明に到達した。
For example, ethylene bisstearylamide is disclosed in Japanese Patent Application Laid-Open No. 51-6
It is produced by the method disclosed in Publication No. 8487, that is, by reacting 2 moles of stearic acid per mole of ethylenediamine, and industrially it is produced by reacting not with stearic acid alone but with a mixed fatty acid mainly composed of stearic acid. The latter, ie, mixed fatty acid amide mainly composed of ethylene bisstearylamide, is used for general antifoaming purposes. In any case, the crystal form u of ethylene bisstearylamide obtained in this way consists of the α type and the β type, with the α type being particularly predominant (US Pat. No. 4,248
(See the specification of No. 792, etc.). The α-type and β-type can be fully distinguished because they have different infrared absorption characteristics at the following wavenumbers. Type Yes None Yes None The inventors of this invention raised a new problem: whether such differences in crystal morphology and their composition ratios have some influence on defoaming performance. As a result of repeated research, research, and consideration, we found that there was a surprising difference in antifoaming performance between the main crystal forms of ethylene bisstearylamide, the α type and the β type, with the β type having better antifoaming properties. It was discovered that the ratio of α type and β type in ethylene bisstearylamide changes due to temperature changes during the production of antifoaming compositions, and this causes fluctuations in antifoaming performance. Reached.

かくしてこの発明によれば、エチレンビスステアリルア
ミドと液体炭化水素油を主成分として含有する消泡用組
成物において、エチレンビスステアリルアミドの80%
以上がβ型エチレンビスステアリルアミドからなること
を特徴とする消泡用組成物が提供される。
Thus, according to the present invention, in an antifoaming composition containing ethylene bis stearylamide and liquid hydrocarbon oil as main components, 80% of the ethylene bis stearyl amide
There is provided an antifoaming composition characterized in that the above is composed of β-type ethylene bisstearylamide.

この発明の消泡用組成物は、含有されているエチレンビ
スステアリルアミド(以下、EBS )中、β型結晶形
を有するものが80%以上を占めており同様な構成の従
来の消泡用組成物に比して消泡性能が著しく優れている
。ことにβ型のEBSが95%以上とすることが消泡性
能の点で好ましく、100%すなわちEBSがすべてβ
型のものであることかより好ましい。
The antifoaming composition of the present invention contains ethylene bisstearylamide (hereinafter referred to as EBS) in which 80% or more has a β-type crystal form, and the antifoaming composition of the present invention has a similar structure to the conventional antifoaming composition. It has significantly better defoaming performance than other products. In particular, it is preferable that the β-type EBS be 95% or more in terms of antifoaming performance.
It is more preferable that it be of a type.

この発明の消泡剤組成物の一成分として使用する液体炭
化水素油としては、芳香族又は脂肪族の何れでもよい。
The liquid hydrocarbon oil used as a component of the antifoam composition of this invention may be either aromatic or aliphatic.

具体的にはヘキサン、ヘプタン、オクタン、ベンゼン、
キシレン、トルエン、パラフィン油、鉱油、ケロシン、
ナフサ等及び石油が挙げられる。これらは2種以上の混
合物であってもよい。通常、安定性の点から粘度10〜
40cps(100’F)のものが好ましい。最も好ま
しい例はパラフィン油である。
Specifically, hexane, heptane, octane, benzene,
xylene, toluene, paraffin oil, mineral oil, kerosene,
Examples include naphtha and petroleum. These may be a mixture of two or more. Usually, from the viewpoint of stability, the viscosity is 10~
40 cps (100'F) is preferred. The most preferred example is paraffin oil.

この発明の消泡用組成物は前記特定のEBSが液体炭化
水素油に懸濁されてなるものである。かような組成物は
、通常市販のEB8を液体炭化水素油に懸濁させ、この
懸濁液を約45〜90℃、好ましくは約70°Cで加熱
処理して、α型優位のEB−8をその80重量%以上が
β型となるように変換調整することにより得られる。具
体的には、例えばEBSの融点付近(約120〜160
℃)に液体炭化水素油を加熱し、これに所望量のFiB
Sを少量ずつ加えて攪拌下BB8を溶解させた後、5− 冷却してEBSが均一に懸濁された組成物とし、これを
約45〜90°C1好ましくは約70℃の温度で加熱処
理することにより得られる。これ以外に、EBSをボー
ルミル等で微粒子状に粉砕した後、液体炭化水素油に加
え、この混合物を攪拌下、約45〜90°C1好ましく
は約70°Cの温度で充分に混和してEBSを懸濁させ
ることにより得られる。通常、EBSを液体炭化水素油
中に溶解させた後熱処理する前者の方法が短時間で行な
えるため簡便で好ましく、ことに溶解時の温度でまずE
BSがほとんどα型になるが、冷却後的70°Cで例え
ば45分〜数時間加熱処理することにより、その80%
以上を短時間でβ型のEB8に変換することができる。
The defoaming composition of the present invention is made by suspending the above-mentioned specific EBS in liquid hydrocarbon oil. Such a composition is usually made by suspending commercially available EB8 in liquid hydrocarbon oil and heat-treating this suspension at about 45 to 90°C, preferably about 70°C, to obtain alpha-predominant EB- It can be obtained by converting and adjusting 8 so that 80% by weight or more of it becomes β type. Specifically, for example, around the melting point of EBS (approximately 120 to 160
℃) and add the desired amount of FiB to it.
After adding S little by little and dissolving BB8 under stirring, 5- cool to obtain a composition in which EBS is uniformly suspended, and heat-treat this at a temperature of about 45 to 90°C, preferably about 70°C. It can be obtained by In addition, EBS is ground into fine particles using a ball mill, etc., and then added to liquid hydrocarbon oil, and the mixture is sufficiently mixed at a temperature of about 45 to 90°C, preferably about 70°C, to form EBS. obtained by suspending. Usually, the former method, in which EBS is dissolved in liquid hydrocarbon oil and then heat-treated, is preferred because it is simple and can be carried out in a short time.
Most of the BS becomes α-type, but 80% of it can be reduced by heat treatment at 70°C for 45 minutes to several hours after cooling.
The above can be converted into β-type EB8 in a short time.

しかし、かような製造法に限定されることなく、例えば
米国特許第4248792号明細書に開示の方法を応用
してもよく少なくとも含有する3BSの80%以上がβ
型FiBSとなるよう調整すればよい。
However, without being limited to such a production method, for example, the method disclosed in US Pat. No. 4,248,792 may be applied. At least 80% or more of the 3BS contained in β
It is only necessary to adjust it so that it becomes a type FiBS.

懸濁させるEBSと液体炭化水素油との配合割合は、通
常、EBSI〜10重量部、液体炭化水6− 素99〜90重量部とするのが適当である。EBSが1
0重量部を越えると得られた組成物の粘度が旨く使用に
際し分散性、取扱い性の点で不都合であり、かつ消泡効
果の向上につながらず不経済である。またEBSが1%
以下では消泡効果が著しく劣り不適当である。なお、こ
の除用いるEBSとして通常市販の工業製品を用いた場
合には前述のように”EBS以外に他の脂肪酸アミド(
012〜22の脂肪酸アミド)が混入し、実質上多成分
の脂肪酸アミドが含有されるが、少なくともEBSが混
合脂肪酸アミドの主体であればよくとくに純粋なEBS
を用いる必要はない。かようなEBSを用いた場合の含
有割合も前記と同様である。
The appropriate blending ratio of EBS and liquid hydrocarbon oil to be suspended is usually ~10 parts by weight of EBSI and 99-90 parts by weight of liquid hydrocarbon. EBS is 1
If it exceeds 0 parts by weight, the viscosity of the resulting composition will be inconvenient in terms of dispersibility and handling when used, and it will not lead to an improvement in the defoaming effect and will be uneconomical. Also, EBS is 1%
Below this, the antifoaming effect will be significantly inferior and unsuitable. In addition, if a commercially available industrial product is used as the EBS to be removed, as mentioned above, other fatty acid amides (
012 to 22 fatty acid amides), and substantially multi-component fatty acid amides are contained, but it is preferable that at least EBS is mainly composed of mixed fatty acid amides, especially pure EBS.
There is no need to use The content ratio when such EBS is used is also the same as above.

このようにしてβ型EBSを80%以上含むEBSと液
体炭化水素油とを主成分として含有するこの発明の消泡
性組成物が得られる。この発明の組成物は、これら2成
分のみから構成されていてもよく、他の公知の補助成分
や添加剤(安定性や消泡性能をより上昇させるためのも
の等)をさらに含有していてもよい。かような補助成分
や添加剤としては、例えば、疎水性シリカ(無機粉末シ
リカの表面にシリコン油を噴霧して焼結してなるもの)
、シリコン油(ジメチルポリシロキサン等のポリシロキ
サン油)、ポリアルキレングリコール(分子量1750
〜8000程度のもの)、プルロニックタイプの消泡剤
、各種分散剤(例えばポリエーテル系ノニオン界面活性
剤等)などが挙げられる。ことにシリコン油を併用した
この発明の消泡性組成物は破泡効果がより上昇するため
好ましいものの一つであり、さらに分散剤を少量含有さ
せると貯蔵安定性もより一様向上する。この際、シリコ
ン油の含有量はEBS+液体炭化水素油の100重量部
に対して1重量部前後が適当であり、分散剤含有量も同
様に約1〜10重量部が適当である。そして分散剤とし
てはそれ自身消泡性能を有してなるプルロニックタイプ
の界面活性剤を用いるのが好適である。
In this way, the antifoaming composition of the present invention containing EBS containing 80% or more of β-type EBS and liquid hydrocarbon oil as main components is obtained. The composition of the present invention may be composed only of these two components, or may further contain other known auxiliary components and additives (such as those for further increasing stability and antifoaming performance). Good too. Such auxiliary components and additives include, for example, hydrophobic silica (made by spraying silicone oil on the surface of inorganic powdered silica and sintering it).
, silicone oil (polysiloxane oil such as dimethylpolysiloxane), polyalkylene glycol (molecular weight 1750
to about 8,000), Pluronic type antifoaming agents, and various dispersants (for example, polyether nonionic surfactants, etc.). In particular, the defoaming composition of the present invention in which silicone oil is used in combination is one of the preferred compositions because the foam-breaking effect is further improved, and furthermore, when a small amount of a dispersant is included, the storage stability is more uniformly improved. At this time, the content of the silicone oil is suitably about 1 part by weight per 100 parts by weight of the EBS+liquid hydrocarbon oil, and the content of the dispersant is similarly suitably about 1 to 10 parts by weight. As the dispersant, it is preferable to use a Pluronic type surfactant which itself has antifoaming properties.

この発明の消泡剤組成物は多くの工業的工程において取
扱われる水性液体又は水性懸濁体、例えばラテックス、
ニカワ、澱粉及び紙パルプ等の製造の発泡性の液に有効
に適用することができる。
The antifoam compositions of this invention are suitable for use in aqueous liquids or aqueous suspensions that are handled in many industrial processes, such as latex,
It can be effectively applied to foaming liquids for manufacturing glue, starch, paper pulp, etc.

この発明の消泡剤組成物の使用濃度は一般に0.01〜
20,000 ppmであり、特にクラフトパルプの製
造における黒液に対しては通常1〜15ppmが用いら
れる。
The concentration of the antifoam composition of this invention is generally from 0.01 to
20,000 ppm, and 1 to 15 ppm is usually used for black liquor, especially in the production of kraft pulp.

以下、この発明を比較例及び実施例によりさらに詳しく
説明するが、これによりこの発明は限定されるものでは
ない。
Hereinafter, this invention will be explained in more detail with reference to comparative examples and examples, but the invention is not limited thereby.

なお、実施例において、エチレンビスステアリルアミド
のα型結晶形のものとβ型結晶形のものとの比率は赤外
吸収スペクトルにおける波数955an−1の吸収と波
数94QCIR−’の吸収の吸収強度により定量を行な
った。その定量法に関する参考例を以下に示す。
In the examples, the ratio between the α-type crystal form and the β-type crystal form of ethylene bisstearylamide is determined by the absorption intensity of the absorption at wave number 955an-1 and the absorption at wave number 94QCIR-' in the infrared absorption spectrum. Quantification was performed. A reference example regarding the quantitative method is shown below.

参考例 第1図〜第5図は、エチレンビスステアリルアミド6g
をヌジョール941とを混合した後、該混合物をボール
ミルで1時間処理してその中のエチレンビスステアリル
アミド粉末を微粉化することにより調製した試料を用い
て測定したエチレン9− ビスステアリルアミドの赤外吸収スペクトル(測定装置
は、日立215型を使用)を示すものである。第1図に
示すのはβ型結晶形が100%のもののIR吸収スペク
トルである。第2図に示すのは、β型結晶形95%、α
型結晶形5%のもの(100%β型結晶形のもの95重
社%と100%β型結晶形のもの5重量%との混合物)
のIR吸収スペクトルである。第8図に示すのはβ型結
晶形80%、α型結晶形20%のもの(混合物)のIR
吸収スペクトルであり第4図に示すのは、β型結晶形5
0%、α型結晶形50%(混合物)。
Reference examples Figures 1 to 5 show 6g of ethylene bisstearylamide.
The infrared radiation of ethylene 9-bis stearylamide was measured using a sample prepared by mixing the mixture with Nujol 941 and then processing the mixture in a ball mill for 1 hour to pulverize the ethylene bis stearylamide powder therein. The absorption spectrum (measurement device used was Hitachi Model 215). What is shown in FIG. 1 is an IR absorption spectrum of 100% β-type crystal form. Figure 2 shows 95% β-type crystal form, α
5% type crystal form (mixture of 95% by weight of 100% β-type crystal form and 5% by weight of 100% β-type crystal form)
This is the IR absorption spectrum of Figure 8 shows the IR of a mixture of 80% β-type crystal and 20% α-type crystal.
The absorption spectrum shown in Figure 4 is β type crystal form 5.
0%, α-form crystal form 50% (mixture).

第5図に示すのは、α型結晶形100%のもののIR吸
収スペクトルである。波数955 clll−’の吸収
と波数94 Q (Im−’の吸収とに着目して、例え
ばβ型結晶形のものの含有率が不明であるエチレンビス
ステアリルアミド試料の赤外吸収スペクトルを第2図或
は第3図と比較することにより、該試料中のβ型結晶形
のものの含有率が80%以上(或は95%以上)である
かどうかを判定することができる。すなわち、該試料の
■几吸収スペクト=10− ルにおける波数955z−’の吸光度に対する波数94
0cm−1の吸光度の比率が第3図の場合よりも大きけ
ればこの試料のβ型結晶含有率は80%よりも大であり
、該比率が第2図の場合よりも大きければこの試料のβ
型結晶含有率は95%よりも大であると判定できる。ま
た波数678m−1の吸収の吸収強度によってもα型結
晶含有率を定量することが可能である。
What is shown in FIG. 5 is an IR absorption spectrum of 100% α-type crystal form. Focusing on the absorption at wave number 955 cll-' and the absorption at wave number 94 Q (Im-'), for example, the infrared absorption spectrum of an ethylene bis stearylamide sample whose content of β-type crystals is unknown is shown in Figure 2. Alternatively, by comparing with FIG. 3, it can be determined whether the content of β-type crystals in the sample is 80% or more (or 95% or more). ■Absorption spectrum = 94 wave number for absorbance of wave number 955z-' at 10-le
If the ratio of absorbance at 0 cm-1 is larger than that in Figure 3, the β-type crystal content of this sample is greater than 80%, and if the ratio is larger than that in Figure 2, the β-type crystal content of this sample is greater than that in Figure 2.
It can be determined that the type crystal content is greater than 95%. It is also possible to quantify the α-type crystal content based on the absorption intensity of absorption at a wave number of 678 m-1.

実施例 試n 1 (比較例1 用試料):エチレンビスステア
リルアミド(アルフローI(508;日本油脂■製−以
F同じ)12vと流動パラフィン30ノとを、外周部に
熱線コイルを巻いた容量800tlの分液漏斗に入れ、
内容物を140〜145°Cの温度に加熱してエチレン
ビスステアリルアミドを流動ハラフィンに溶解させた。
Example sample n 1 (Sample for Comparative Example 1): 12 volts of ethylene bisstearylamide (Alflo I (508; manufactured by NOF ■ - same as F) and 30 volts of liquid paraffin, with a hot wire coil wrapped around the outer periphery. Pour into an 800 tl separatory funnel,
The contents were heated to a temperature of 140-145°C to dissolve the ethylene bisstearylamide in the liquid halafin.

別に、流動パラフィン158gを入れたフラスコを、食
塩を添加された氷冷水浴にて一10°Cに冷却しておき
、上記の加熱されたエチレンビスステアリルアミド溶液
を徐々にフラスコ内に滴下した。該溶液を滴下している
間はフラスコ内容物の温度が5°C以下に保たれるよう
に滴下速度を調節した。滴下完了後、5℃以下の温度で
1時間該フラスコ内容物を攪拌し、更に内容物をフラス
コからとり出してボールミルで1時間処理し、エチレン
ビスステアリルアtFが均一に分散した消泡用組成物を
得た。この組成物ハエチレンビスステアリルアミド6重
量%、流動ハラフィン94重量%より成り、エチレンビ
スステアリルアミドはα型結晶形のものが100%を占
めていた。
Separately, a flask containing 158 g of liquid paraffin was cooled to -10°C in an ice-cold water bath to which common salt had been added, and the heated ethylene bisstearylamide solution was gradually dropped into the flask. While the solution was being added dropwise, the dropping rate was adjusted so that the temperature of the contents of the flask was maintained below 5°C. After completion of the dropwise addition, the contents of the flask were stirred for 1 hour at a temperature of 5° C. or lower, and the contents were further taken out of the flask and treated in a ball mill for 1 hour to obtain an antifoaming composition in which ethylene bisstearyl atF was uniformly dispersed. I got something. This composition consisted of 6% by weight of ethylenebisstearylamide and 94% by weight of fluid halafin, and 100% of the ethylenebisstearylamide was in the α-type crystal form.

試料2(比較例2用試料):エチレンビスステアリルア
ミド12jlと流動パラフィン30gとを、外周部に熱
線コイルを巻いた容量800sglの分液漏斗に入れ、
内容物を140〜145℃の温度に加熱してエチレンビ
スステアリルアミドを流動ハラフィンに溶解させた。別
に、流動パラフィン158ノを入れたフラスコを水浴に
て40℃に加熱しておき、上記の加熱されたエチレンビ
スステアリルアミド溶液を徐々にフラスコ内に滴下した
Sample 2 (sample for Comparative Example 2): 12 jl of ethylene bisstearylamide and 30 g of liquid paraffin were placed in a separatory funnel with a capacity of 800 sgl and a hot wire coil was wound around the outer periphery.
The contents were heated to a temperature of 140-145°C to dissolve the ethylene bisstearylamide into the liquid halafin. Separately, a flask containing 158 g of liquid paraffin was heated to 40° C. in a water bath, and the heated ethylene bisstearylamide solution was gradually dropped into the flask.

該溶液を滴下している間はフラスコ内容物の温度が70
℃以下に保たれるように滴下速度を調節した。滴下完了
後、70°C±2℃の温度で80分間該フラスコ内容物
を攪拌し、次に攪拌しながら25℃まで放冷し、更に内
容物をフラスコからとす出してボールミルで1時間処理
し、エチレンビスステアリルアミドが均一に分散した消
泡用組成物ヲ得た。この組成物はエチレンビスステアリ
ルアミド6重量%、流動パラフィン94重量%より成り
、エチレンビスステアリルアミドはα型結晶形45重量
%、β型結晶形55重量%の混合物であった。
While the solution was being added dropwise, the temperature of the contents of the flask was 70°C.
The dropping rate was adjusted to maintain the temperature below ℃. After the addition was completed, the contents of the flask were stirred at a temperature of 70°C ± 2°C for 80 minutes, then allowed to cool to 25°C while stirring, and the contents were taken out of the flask and processed in a ball mill for 1 hour. An antifoaming composition in which ethylene bisstearylamide was uniformly dispersed was obtained. This composition consisted of 6% by weight of ethylene bis-stearylamide and 94% by weight of liquid paraffin, and the ethylene bis-stearylamide was a mixture of 45% by weight of α-type crystal form and 55% by weight of β-type crystal form.

試料8(実施例1用試料):エチレンビスステアリルア
ミド12Fと流動パラフィン30fとを、外周部に熱線
コイルを巻いた容量800s+7の分液漏斗に入れ、内
容物を140〜145°Cの温度に加熱してエチレンビ
スステアリルアミドを流動パラフィンに溶解させた。別
に、流動パラフィン158gを入れたフラスコを水浴に
て40°Cに加熱しておき、上記の加熱されたエチレン
ビスステアリルアミド溶液を徐々にフラスコ内に滴下し
た。
Sample 8 (sample for Example 1): 12F of ethylene bisstearylamide and 30F of liquid paraffin were placed in a separatory funnel with a capacity of 800s+7 with a hot wire coil wound around the outer periphery, and the contents were brought to a temperature of 140 to 145°C. The ethylene bisstearylamide was dissolved in the liquid paraffin by heating. Separately, a flask containing 158 g of liquid paraffin was heated to 40°C in a water bath, and the heated ethylene bisstearylamide solution was gradually dropped into the flask.

18− 該溶液を滴下している間はフラスコ内容物の温度が70
℃以下に保たれるように滴下速度を調節した。滴下完了
後、70°C±2°Cの温度で45分間該フラスコ内容
物を攪拌し、次に攪拌しながら25℃まで放冷し、更に
内容物をフラスコからとり出してボールミルで1時間処
理し7、エチレンビスステアリルアミドが均一に分散し
た消泡用組成物を得た。この組成物はエチレンビスステ
アリルアミド6重量%、流動パラフィン94重量%より
成す、エチレンビスステアリルアミドはα型結晶形17
重量%、β型結晶形88重量%の混合物であった。
18- While the solution is being added dropwise, the temperature of the contents of the flask is 70°C.
The dropping rate was adjusted to maintain the temperature below ℃. After the addition was completed, the contents of the flask were stirred at a temperature of 70°C ± 2°C for 45 minutes, then allowed to cool to 25°C while stirring, and the contents were taken out of the flask and processed in a ball mill for 1 hour. 7. An antifoaming composition in which ethylene bisstearylamide was uniformly dispersed was obtained. This composition consists of 6% by weight of ethylene bisstearylamide and 94% by weight of liquid paraffin.
It was a mixture of 88% by weight of β type crystal form.

試料4(実施例2用試料):エチレンビスステアリルア
ミド12Fと流動パラフィン30gとを、外周部に熱線
コイルを巻いた容量800 mlの分液漏斗に入れ、内
容物を140〜145°Cの温度に加熱してエチレンビ
スステアリルアミドを流動パラフィンに溶解させた。別
に、流動パラフィン158fを入れたフラスコを水浴に
て40℃に加熱しておき、上記の加熱されたエチレンビ
スステー14= アリルアミド溶液を徐々にフラスコ内に滴下した。
Sample 4 (sample for Example 2): Ethylene bisstearylamide 12F and 30 g of liquid paraffin were placed in an 800 ml separating funnel with a hot wire coil wrapped around the outer periphery, and the contents were brought to a temperature of 140 to 145°C. The ethylene bisstearylamide was dissolved in the liquid paraffin by heating to . Separately, a flask containing liquid paraffin 158f was heated to 40° C. in a water bath, and the heated ethylene bis-stay 14=allylamide solution was gradually dropped into the flask.

該溶液を滴下している間はフラスコ内容物の温度が70
°C以下に保たれるように滴下速度を調節した。滴下完
了後、70°C±2°Cの温度で90分間該フラスコ内
容物を攪拌し、次に攪拌しなから25°Cまで放冷し、
更に内容物をフラスコからとり出してボールミルで1時
間処理し、エチレンビスステアリルアミドが均一に分散
した消泡用組成物を得た。この組成物はエチレンビスス
テアリルアミド6重量%、流動パラフィン94重量%よ
り成す、エチレンビスステアリルアミドはa型結晶形5
重量%以下、β型結晶形95重量%以上の混合物であっ
た。
While the solution was being added dropwise, the temperature of the contents of the flask was 70°C.
The dropping rate was adjusted to remain below °C. After completion of the addition, the contents of the flask were stirred for 90 minutes at a temperature of 70°C ± 2°C, then allowed to cool to 25°C without stirring,
Further, the contents were taken out from the flask and treated in a ball mill for 1 hour to obtain an antifoaming composition in which ethylene bisstearylamide was uniformly dispersed. This composition consists of 6% by weight of ethylene bisstearylamide and 94% by weight of liquid paraffin.
It was a mixture containing 95% by weight or less of the β-type crystal form.

試料5(実施例3用試料):エチレンビスステアリルア
ミド12yと流動パラフィン30gとを、外周部に熱線
コイルを巻いた容量800m/の分液漏斗に入れ、内容
物を140〜145°Cの温度に加熱してエチレンビス
ステアリルアミドを流動パラフィンに溶解させた。別に
、流動パラフィン158fを入れたフラスコを水浴にて
40°Cに加熱しておき、上記の加熱されたエチレンビ
スステアリルアミド溶液を徐々にフラスコ内に滴下した
Sample 5 (sample for Example 3): 12y of ethylene bisstearylamide and 30g of liquid paraffin were placed in a separatory funnel with a capacity of 800m/volume wrapped around a hot wire coil, and the contents were heated to a temperature of 140 to 145°C. The ethylene bisstearylamide was dissolved in the liquid paraffin by heating to . Separately, a flask containing 158f of liquid paraffin was heated to 40°C in a water bath, and the heated ethylene bisstearylamide solution was gradually dropped into the flask.

該溶液を滴下している間はフラスコ内容物の温度が70
°C以下に保たれるように滴下速度を調節した。滴下完
了後、70″C±2°Cの温度で5時間該フラスコ内容
物を攪拌し、次に攪拌しなから25°Cまで放冷し、更
に内容物をフラスコからとり出してボールミルで1時間
処理し、エチレンビスステアリルアミドが均一に分散し
た消泡用組成物を得た。この組成物はエチレンビスステ
アリルアミド6重量%、流動パラフィン94重量%より
成り、エチレンビスステアリルアミドはβ型結晶形のも
のが100%を占めていた。
While the solution was being added dropwise, the temperature of the contents of the flask was 70°C.
The dropping rate was adjusted to remain below °C. After the addition was completed, the contents of the flask were stirred for 5 hours at a temperature of 70"C ± 2°C, then allowed to cool to 25°C without stirring, and the contents were taken out of the flask and milled in a ball mill for 1 hour. A defoaming composition in which ethylene bis stearylamide was uniformly dispersed was obtained by time treatment. This composition consisted of 6% by weight of ethylene bis stearylamide and 94% by weight of liquid paraffin. Shape accounted for 100%.

〔消泡性能試験〕[Defoaming performance test]

基パルプ工場で生ずる蒸解後黒液(pH1,2,8、固
形分含有率25.7重量%)を固形分含有率が10重量
%になるように純水で稀釈して得られた液500−を、
内径6.31の円筒状容器(例えばメスシリンダーのよ
うな形のもの)に入れて75℃の温度に保ち、この液に
対し消泡用組成物9 ppm(重量)を添加した。この
容器の底部から、この液に対して毎分1120°C)の
割合で空気を通じて液を泡立たせ、通気開始から泡の体
積が100ゴ、800m/、或は500耐に達するのに
要する時間を測定し、この時間が長いものを消泡性能が
優れていると判定した。
A liquid obtained by diluting the black liquor (pH 1, 2, 8, solids content 25.7% by weight) produced at the base pulp mill with pure water to a solids content of 10% by weight. −,
The solution was placed in a cylindrical container (for example, shaped like a graduated cylinder) with an inner diameter of 6.31 mm and maintained at a temperature of 75° C., and 9 ppm (by weight) of an antifoaming composition was added to the solution. Air is bubbled through the liquid from the bottom of the container at a rate of 1120°C per minute, and the time required from the start of ventilation until the volume of the bubbles reaches 100 g, 800 m/min, or 500 g/min. was measured, and those with a long time were judged to have excellent defoaming performance.

得られた結果を第1表に示す。The results obtained are shown in Table 1.

第1表 以上の結果から、エチレンビスステアリルアミド中のβ
型結晶形のものの含有率が80%以上に17− なると消泡性能が著しく改善され、β型結晶形のものの
含有率が95重量%以上になるとβ型結晶形が100%
のものと実質上差が認められない程優れた消泡性能を示
すことが判る。
From the results in Table 1 and above, β in ethylene bisstearylamide
When the content of β-type crystals is 80% or more, the defoaming performance is significantly improved, and when the content of β-type crystals is 95% or more by weight, β-type crystals become 100%.
It can be seen that the antifoaming performance is so excellent that there is virtually no discernible difference between the two.

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

第1図はβ型結晶形が100%を占めるエチレンビスス
テアリルアミドの赤外吸収スペクトルを示す図である。 第2図はα型結晶形5重量%、β型結晶形95重量%の
エチレンビスステアリルアミドの脈外吸収スペクトルを
示す図である。第8図はα型結晶形20重量%、β型結
晶形80重量%のエチレンビスステアリルアミドの赤外
吸収スペクトルを示す図である。第4図はα型結晶形5
0重量%、β型結晶形50重散%のエチレンビスステア
リルアミドの赤外吸収スペクトルを示す図である。第5
図はα型結晶形が100%を占めるエチレンビスステア
リルアミドの赤外吸収スペクトルを示す図である。 18−
FIG. 1 is a diagram showing an infrared absorption spectrum of ethylene bisstearylamide in which the β-type crystal form accounts for 100%. FIG. 2 is a diagram showing an extravascular absorption spectrum of ethylene bisstearylamide containing 5% by weight of α type crystal form and 95% by weight of β type crystal form. FIG. 8 is a diagram showing an infrared absorption spectrum of ethylene bisstearylamide containing 20% by weight of α type crystal and 80% by weight of β type crystal. Figure 4 shows α-type crystal form 5.
FIG. 2 is a diagram showing an infrared absorption spectrum of ethylene bisstearylamide with 0% by weight and 50% β-type crystal form. Fifth
The figure shows an infrared absorption spectrum of ethylene bis stearylamide in which the α-type crystal form accounts for 100%. 18-

Claims (1)

【特許請求の範囲】 1、エチレンビスステアリルアミドと液体炭化水素油を
主成分として含有する消泡用組成物において、エチレン
ビスステアリルアミドの80%以上がβ型エチレンビス
ステアリルアミドからなることを特徴とする消泡用組成
物。 2、 エチレンビスステアリルアミドを液体炭化水素油
に懸濁させ、この懸濁液を約45〜90°Cに加熱処理
することによりエチレンビスステアリルアミド中のβ型
エチレンヒスステアリルアミド含量を80%以上に父換
調整することを特徴とする消泡用組成物の製造法。
[Claims] 1. An antifoaming composition containing ethylene bis stearylamide and liquid hydrocarbon oil as main components, characterized in that 80% or more of the ethylene bis stearyl amide is composed of β-type ethylene bis stearyl amide. A defoaming composition. 2. By suspending ethylene bis stearylamide in liquid hydrocarbon oil and heating this suspension at about 45 to 90°C, the content of β-type ethylene his stearylamide in ethylene bis stearylamide is reduced to 80% or more. 1. A method for producing an antifoaming composition, which is characterized by adjusting the father exchange rate.
JP14527082A 1982-08-20 1982-08-20 Composition for defoaming and its production Granted JPS5936509A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14527082A JPS5936509A (en) 1982-08-20 1982-08-20 Composition for defoaming and its production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14527082A JPS5936509A (en) 1982-08-20 1982-08-20 Composition for defoaming and its production

Publications (2)

Publication Number Publication Date
JPS5936509A true JPS5936509A (en) 1984-02-28
JPS646803B2 JPS646803B2 (en) 1989-02-06

Family

ID=15381247

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14527082A Granted JPS5936509A (en) 1982-08-20 1982-08-20 Composition for defoaming and its production

Country Status (1)

Country Link
JP (1) JPS5936509A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012031543A (en) * 2010-08-01 2012-02-16 San Nopco Ltd Antifoaming agent for kraft pulp production process

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02148220U (en) * 1989-05-20 1990-12-17
JPH0385808U (en) * 1989-12-22 1991-08-30

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3723342A (en) * 1971-12-21 1973-03-27 Hart Chemical Ltd Defoamer composition
US3935121A (en) * 1973-06-29 1976-01-27 Betz Laboratories, Inc. Foam control compositions for aqueous systems, its preparation, and process using same
JPS5222356A (en) * 1975-08-13 1977-02-19 Nishihara Environ Sanit Res Corp Digesting process of contaminated organic liquid and equipment therefo r
US4248792A (en) * 1979-06-22 1981-02-03 Glyco Chemicals, Inc. Process for the interconversion of crystalline forms of ethylene bis-stearamide

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3723342A (en) * 1971-12-21 1973-03-27 Hart Chemical Ltd Defoamer composition
US3935121A (en) * 1973-06-29 1976-01-27 Betz Laboratories, Inc. Foam control compositions for aqueous systems, its preparation, and process using same
JPS5222356A (en) * 1975-08-13 1977-02-19 Nishihara Environ Sanit Res Corp Digesting process of contaminated organic liquid and equipment therefo r
US4248792A (en) * 1979-06-22 1981-02-03 Glyco Chemicals, Inc. Process for the interconversion of crystalline forms of ethylene bis-stearamide

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012031543A (en) * 2010-08-01 2012-02-16 San Nopco Ltd Antifoaming agent for kraft pulp production process

Also Published As

Publication number Publication date
JPS646803B2 (en) 1989-02-06

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