JPS6253203B2 - - Google Patents

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Publication number
JPS6253203B2
JPS6253203B2 JP6911779A JP6911779A JPS6253203B2 JP S6253203 B2 JPS6253203 B2 JP S6253203B2 JP 6911779 A JP6911779 A JP 6911779A JP 6911779 A JP6911779 A JP 6911779A JP S6253203 B2 JPS6253203 B2 JP S6253203B2
Authority
JP
Japan
Prior art keywords
weight
parts
hlb
distillate
tall oil
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.)
Expired
Application number
JP6911779A
Other languages
Japanese (ja)
Other versions
JPS55159810A (en
Inventor
Kunio Arimoto
Hisao Irie
Masahisa Ishigami
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.)
Harima Chemicals Inc
Original Assignee
Harima Chemicals 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 Harima Chemicals Inc filed Critical Harima Chemicals Inc
Priority to JP6911779A priority Critical patent/JPS55159810A/en
Publication of JPS55159810A publication Critical patent/JPS55159810A/en
Publication of JPS6253203B2 publication Critical patent/JPS6253203B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は紙パルプ工業における水系の発泡を防
止する消泡剤に関するものである。 紙パルプ工業における発泡は、サイズ剤、バン
ド、澱粉、樹脂分、カゼイン、酸化チタン、タル
ク、クレー、染料等の添加に起因し、そのため生
産能率低下、生産材料の損失、生産機械にあたえ
る損害、排水公害をきたす。 今日まで泡対策として、鉱物油、パラフイン、
シリコーン樹脂、高級アルコール、脂肪酸エステ
ル、非イオン活性剤などの消泡剤が使用されてき
たが、鉱物油、パラフイン、高級アルコールは水
に不溶であるため速効性に乏しく、かつ繊維への
付着による障害をおこし、シリコーン樹脂は消泡
効果は良いが価格が高く、その使用は制限され、
又非イオン活性剤は水系への分散は良好である
が、一般にその効果が乏しい、などそれぞれ欠点
がある。 一方又、脂肪酸エステルの中でもグリセリンモ
ノエステルは鉱油、ワツクスと組み合せるとその
効果が大であり、このことはU.S.P2715614にも
記載されている。しかし、ステアリン酸、オレイ
ン酸のモノグリセライドは消泡効果に乏しく、ス
テアリン酸、オレイン酸のモノグリセライドに鉱
油やワツクスを添加すれば、消泡効果は増すが、
その時多量の水で希釈されると沈積物をつくり、
繊維付着を起こすという欠点を有している。 このような欠点をなくすべく、種々検討の結
果、酸価90〜170のトール油初留分とグリセリン
とのモノエステル又はジエステル又はこれらの混
合物100重量部に対して、0・5〜30重量部の脂
肪酸アルカリ塩、HLB9.0以上の脂肪酸のポリア
ルキレングリコールエステル、HLB9.0以上の樹
脂酸のポリアルキレングリコールエステル及び
HLB9.0以上の脂肪酸の多価アルコールエステル
よりなる群より選ばれた1種又は2種以上からな
る乳化剤を添加混合し、HLB2.4〜4.0に調節した
消泡剤は、破泡と抑泡の両作用を有し、持続性に
もすぐれ、多量の水で希釈しても沈積物を作らな
いということを見出し、本発明を完成した。 本発明に使用するトール油初留分は、パルミチ
ン酸、オレイン酸などの脂肪酸を50〜80重量%、
不ケン化物を20〜50重量%含む。トール油初留分
中の不ケン化物は、鉱油やワツクスのように多量
の水で希釈しても沈積物を作らず、消泡効果を増
大させる。 トール油初留分の酸価の下限を90に規定したの
は、粗トール油精留器の一般的能力からみて、こ
れより低い酸価の初留分を得ることは操業効率上
困難が伴い工業的経済性に欠けるためであり、且
又酸価90以上でなければグリセリンエステル濃度
が減少し消泡能力が低下するためである。又上限
を170に限定したのは、この値をこえると消泡剤
のHLB価が高くなり消泡剤効果が乏しくなるた
めである。 又ここで脂肪酸又は樹脂酸のポリアルキレング
リコールエステル及び脂肪酸の多価アルコールエ
ステルのHLBを9.0以上とした理由は、このHLB
が9.0以下であると、乳化剤としての働きが不十
分で系の乳化が困難であるからである。 又乳化剤を0.5〜30重量部に限定した理由は、
30重量部以上は不要であり、かえつて製品の発泡
防止能力が減少し、0.5重量部以下では均一な乳
化系液がえにくいからである。 更に又混合系のHLBを2.4〜4.0と限定したの
は、2.4以下のときは消泡効果が乏しく、又4.0以
上のときは消泡剤としての働きが劣りかえつて発
泡し易くなるからである。 本発明によれば、秀れた消泡剤は、例えば、酸
価90〜170のトール油初留分100重量部に対して、
グリセリン7〜30重量部を加え、200〜250℃で2
〜8時間反応後、得られた反応生成物100重量部
に対して0.5〜30重量部の乳化剤を加えた後、水
を加えて乳化することにより容易に得られる。 又乳化剤に脂肪酸のポリアルキレングリコール
エステルあるいは多価アルコールエステルを使用
する時には、グリセリンと同時に仕込み反応させ
ても、同一の目的物が得られる。 以下実施例により本発明を説明する。 実施例 1 撹拌装置、凝縮装置を付した反応容器に酸価
165のトール油初留分100重量部、グリセリン27重
量部、ポリエチレングリコール(平均分子量
1000)0.7重量部を入れ、チツソガス下に235℃に
昇温し、235℃で2時間加熱を続け、トール油初
留分のグリセリンモノエステルとトール油初留分
のポリエチレングリコールモノエステルとの重量
比が99:1に相当する反応生成物120重量部を得
た。この反応生成物100重量部を乳化釜に移し、
液温を70℃に保ちながら撹拌下に熱水400重量部
を加えて消泡剤Aを得た。(HLB3.0) 実施例 2 実施例1記載の反応容器に酸価90のトール油初
留分100重量部、グリセリン11重量部を仕込み、
チツソガス下に250℃で6時間加熱を続け、トー
ル油初留分グリセリンモノエステルとトール油初
留分グリセリンジエステルの重量比が1:1に相
当する反応生成物105重量部を得た。この反応生
成物100重量部を乳化釜に移し、HLB12.0のトー
ルロジンのポリエチレングリコール(平均分子量
460)エステル27重量部を加え、液温を70℃に保
ちながら撹拌下に熱水508重量部を加えて消泡剤
Bを得た。(HLB3.7) 実施例 3 実施例2と同一の反応生成物100重量部を乳化
釜に入れ、HLB12.0のトールロジンのポリエチレ
ングリコール(平均分子量460)エステル2.1重量
部を加え液温を70℃に保ちながら撹拌下に熱水
408重量部を加えて消泡剤Cを得た。(HLB2.6) 実施例 4 実施例1と同一反応装置に酸価140のトール油
初留分100重量部に対してグリセリン11.5重量部
を仕込み、チツソガス下に235℃で6時間加熱を
続け、トール油初留分のグリセリンジエステル
105重量部を得た。この反応生成物100重量部を乳
化釜に移し、オレイン酸カリウム12.4重量部を加
え、液温を70℃に保ちながら撹拌下に熱水450重
量部を加えて消泡剤Dを得た。(HLB3.0) 比較例 モノグリセリルステアレートを比較消泡剤Eと
した。 実施例 5 消泡試験 ロジン系サイズ剤HR−50(播磨化成工業(株)
製)を精製水で固形分濃度2%になるように希釈
し、2%硫酸アルミニウム水溶液を撹拌下に加
え、PH9.0、7.0、5.0に調整した液を発泡液とし
た。発泡液300gを計量し、水で希釈した消泡剤
をホールピペツトで所定量添加し、混合した。ロ
スマイルス法(JIS K−3362)にて5分後の泡高
を測定した。その結果を表1、2、3に示す。
The present invention relates to antifoaming agents for preventing aqueous foaming in the pulp and paper industry. Foaming in the pulp and paper industry is caused by the addition of sizing agents, bands, starches, resins, casein, titanium oxide, talc, clay, dyes, etc., resulting in decreased production efficiency, loss of production materials, damage to production machinery, Causes wastewater pollution. To date, mineral oil, paraffin,
Antifoaming agents such as silicone resins, higher alcohols, fatty acid esters, and nonionic activators have been used, but mineral oils, paraffin, and higher alcohols are insoluble in water, so they lack quick effectiveness, and they tend to adhere to fibers. Although silicone resin has a good antifoaming effect, it is expensive and its use is limited.
In addition, although nonionic surfactants have good dispersibility in aqueous systems, they each have drawbacks such as generally poor effectiveness. On the other hand, among fatty acid esters, glycerin monoester has a great effect when combined with mineral oil or wax, and this is also described in USP 2715614. However, monoglycerides of stearic acid and oleic acid have poor antifoaming effects, and adding mineral oil or wax to monoglycerides of stearic acid and oleic acid increases the antifoaming effect, but
If it is diluted with a large amount of water, it will form a deposit,
It has the disadvantage of causing fiber adhesion. In order to eliminate such drawbacks, as a result of various studies, 0.5 to 30 parts by weight of a monoester or diester of tall oil first distillate with an acid value of 90 to 170 and glycerin, or a mixture thereof, is added to 100 parts by weight. alkali salts of fatty acids, polyalkylene glycol esters of fatty acids with HLB 9.0 or more, polyalkylene glycol esters of resin acids with HLB 9.0 or more, and
An antifoaming agent containing one or more emulsifiers selected from the group consisting of polyhydric alcohol esters of fatty acids with an HLB of 9.0 or higher and adjusted to an HLB of 2.4 to 4.0 has the ability to break foam and suppress foam. The present invention was completed based on the discovery that it has both of the following effects, has excellent sustainability, and does not form deposits even when diluted with a large amount of water. The tall oil first distillate used in the present invention contains 50 to 80% by weight of fatty acids such as palmitic acid and oleic acid.
Contains 20-50% by weight of unsaponifiables. Unsaponifiable substances in the first distillate of tall oil do not form deposits like mineral oil or wax even when diluted with a large amount of water, increasing the antifoaming effect. The lower limit of the acid value of the first distillate of tall oil was set at 90 because, given the general capacity of the crude tall oil rectifier, it would be difficult to obtain a first distillate with an acid value lower than this in terms of operational efficiency. This is because it lacks industrial economic efficiency, and if the acid value is not 90 or higher, the glycerin ester concentration decreases and the defoaming ability decreases. The reason why the upper limit is limited to 170 is that if this value is exceeded, the HLB value of the antifoaming agent becomes high and the antifoaming effect becomes poor. Also, the reason why the HLB of the polyalkylene glycol ester of fatty acid or resin acid and the polyhydric alcohol ester of fatty acid was set to 9.0 or more is that this HLB
If it is less than 9.0, its function as an emulsifier is insufficient and it is difficult to emulsify the system. The reason why the emulsifier is limited to 0.5 to 30 parts by weight is as follows.
It is unnecessary to use more than 30 parts by weight, as it will actually reduce the foaming prevention ability of the product, and if less than 0.5 parts by weight, it will be difficult to obtain a uniform emulsified liquid. Furthermore, the reason why the HLB of the mixed system is limited to 2.4 to 4.0 is that when it is less than 2.4, the antifoaming effect is poor, and when it is more than 4.0, the antifoaming effect is poor and foaming becomes more likely. . According to the present invention, the excellent antifoaming agent is, for example, based on 100 parts by weight of tall oil initial distillate having an acid value of 90 to 170.
Add 7 to 30 parts by weight of glycerin and heat at 200 to 250℃ for 2 hours.
After reaction for ~8 hours, 0.5 to 30 parts by weight of an emulsifier is added to 100 parts by weight of the obtained reaction product, and then water is added and emulsified to easily obtain the product. Furthermore, when a polyalkylene glycol ester or polyhydric alcohol ester of a fatty acid is used as an emulsifier, the same desired product can be obtained even if it is charged and reacted simultaneously with glycerin. The present invention will be explained below with reference to Examples. Example 1 Acid value was set in a reaction vessel equipped with a stirring device and a condensing device.
100 parts by weight of tall oil first distillate of No. 165, 27 parts by weight of glycerin, polyethylene glycol (average molecular weight
Add 0.7 parts by weight of 1000), raise the temperature to 235℃ under Chituso gas, continue heating at 235℃ for 2 hours, and calculate the weight of glycerin monoester of tall oil first distillate and polyethylene glycol monoester of tall oil first distillate. 120 parts by weight of reaction product were obtained, corresponding to a ratio of 99:1. Transfer 100 parts by weight of this reaction product to an emulsification pot,
Antifoaming agent A was obtained by adding 400 parts by weight of hot water while stirring while maintaining the liquid temperature at 70°C. (HLB3.0) Example 2 Into the reaction vessel described in Example 1, 100 parts by weight of tall oil first distillate with an acid value of 90 and 11 parts by weight of glycerin were charged.
Heating was continued at 250° C. for 6 hours under Tituso gas to obtain 105 parts by weight of a reaction product corresponding to a weight ratio of 1:1 of tall oil first distillate glycerin monoester and tall oil first distillate glycerin diester. 100 parts by weight of this reaction product was transferred to an emulsification pot, and the polyethylene glycol of tall rosin (average molecular weight
460) Antifoaming agent B was obtained by adding 27 parts by weight of ester and adding 508 parts by weight of hot water while stirring while keeping the liquid temperature at 70°C. (HLB3.7) Example 3 Put 100 parts by weight of the same reaction product as in Example 2 into an emulsification pot, add 2.1 parts by weight of tall rosin polyethylene glycol (average molecular weight 460) ester with HLB 12.0, and raise the liquid temperature to 70°C. Add hot water under stirring while keeping
Antifoaming agent C was obtained by adding 408 parts by weight. (HLB2.6) Example 4 In the same reaction apparatus as in Example 1, 11.5 parts by weight of glycerin was charged to 100 parts by weight of the first distillate of tall oil with an acid value of 140, and heating was continued at 235°C for 6 hours under Chituso gas. Glycerin diester of tall oil first distillate
105 parts by weight were obtained. 100 parts by weight of this reaction product was transferred to an emulsification tank, 12.4 parts by weight of potassium oleate was added, and 450 parts by weight of hot water was added while stirring while maintaining the liquid temperature at 70°C to obtain antifoaming agent D. (HLB3.0) Comparative Example Monoglyceryl stearate was used as comparative antifoaming agent E. Example 5 Defoaming test Rosin-based sizing agent HR-50 (Harima Kasei Kogyo Co., Ltd.)
2% aluminum sulfate aqueous solution was added under stirring to adjust the pH to 9.0, 7.0, and 5.0, which was used as a foaming solution. 300 g of the foaming liquid was weighed, and a predetermined amount of an antifoaming agent diluted with water was added using a whole pipette and mixed. The foam height after 5 minutes was measured using the Ross Miles method (JIS K-3362). The results are shown in Tables 1, 2, and 3.

【表】【table】

【表】【table】

【表】 実施例 6 サイズ度試験 針葉樹晒パルプ抄紙用スラリー中に、ロジン系
サイズ剤HR−50(播磨化成工業(株)製)を、固形
分として0.5重量%を含有する量を添加混合し、
得られたスラリーに抄紙直前時に消泡剤A〜Dを
スラリー中のパルプ分に対して0.05〜0.2重量%
添加混合した。このとき何れも発泡は起こらず、
沈積物もなく、サイズ度の低下も、みられなかつ
た。
[Table] Example 6 Sizing test A rosin-based sizing agent HR-50 (manufactured by Harima Kasei Kogyo Co., Ltd.) was added and mixed in an amount containing 0.5% by weight as solid content into a slurry of bleached softwood pulp for paper making. ,
Immediately before paper making, antifoaming agents A to D are added to the resulting slurry in an amount of 0.05 to 0.2% by weight based on the pulp content in the slurry.
Add and mix. At this time, no foaming occurred,
There was no deposit and no decrease in size was observed.

Claims (1)

【特許請求の範囲】[Claims] 1 酸価90〜170のトール油初留分とグリセリン
とのモノエステル又はジエステル又はこれらの混
合物100重量部に対して、0・5〜30重量部の脂
肪酸アルカリ塩、HLB9.0以上の脂肪酸又は樹脂
酸のポリアルキレングリコールエステル、及び
HLB9.0以上の脂肪酸の多価アルコールエステル
よりなる群より選ばれた1種又は2種以上からな
る乳化剤を添加混合し、HLB2.4〜4.0に調節する
ことを特徴とする紙パルプ製造工程用消泡剤。
1. 0.5 to 30 parts by weight of a fatty acid alkali salt, a fatty acid with an HLB of 9.0 or more, or polyalkylene glycol esters of resin acids, and
For a paper pulp manufacturing process characterized by adding and mixing an emulsifier consisting of one or more selected from the group consisting of polyhydric alcohol esters of fatty acids with an HLB of 9.0 or higher to adjust the HLB to 2.4 to 4.0. Antifoaming agent.
JP6911779A 1979-06-01 1979-06-01 Defoaming agent for paper pulp manufacturing process Granted JPS55159810A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6911779A JPS55159810A (en) 1979-06-01 1979-06-01 Defoaming agent for paper pulp manufacturing process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6911779A JPS55159810A (en) 1979-06-01 1979-06-01 Defoaming agent for paper pulp manufacturing process

Publications (2)

Publication Number Publication Date
JPS55159810A JPS55159810A (en) 1980-12-12
JPS6253203B2 true JPS6253203B2 (en) 1987-11-09

Family

ID=13393370

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6911779A Granted JPS55159810A (en) 1979-06-01 1979-06-01 Defoaming agent for paper pulp manufacturing process

Country Status (1)

Country Link
JP (1) JPS55159810A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0686553U (en) * 1993-05-27 1994-12-20 有限会社シンク Storage

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4127719A1 (en) * 1991-08-22 1993-02-25 Basf Ag A DECISIVE FOR THE PAPER INDUSTRY BASED ON OIL-IN-WATER EMULSIONS

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0686553U (en) * 1993-05-27 1994-12-20 有限会社シンク Storage

Also Published As

Publication number Publication date
JPS55159810A (en) 1980-12-12

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