JPH0324126A - Polymerized fatty acid ester and deinking of waste-paper by using same - Google Patents

Polymerized fatty acid ester and deinking of waste-paper by using same

Info

Publication number
JPH0324126A
JPH0324126A JP1159038A JP15903889A JPH0324126A JP H0324126 A JPH0324126 A JP H0324126A JP 1159038 A JP1159038 A JP 1159038A JP 15903889 A JP15903889 A JP 15903889A JP H0324126 A JPH0324126 A JP H0324126A
Authority
JP
Japan
Prior art keywords
deinking
fatty acid
acid
ink
paper
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
JP1159038A
Other languages
Japanese (ja)
Inventor
Takashi Yamashita
隆 山下
Eigo Tsuchiya
土屋 栄吾
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.)
Ajinomoto Co Inc
Original Assignee
Ajinomoto Co 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 Ajinomoto Co Inc filed Critical Ajinomoto Co Inc
Priority to JP1159038A priority Critical patent/JPH0324126A/en
Publication of JPH0324126A publication Critical patent/JPH0324126A/en
Pending legal-status Critical Current

Links

Classifications

    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/50—Reuse, recycling or recovery technologies
    • Y02W30/64—Paper recycling

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  • Paper (AREA)
  • Polyethers (AREA)

Abstract

PURPOSE:To obtain a deinking agent which has an excellent ability to release an ink from wastepaper and an ability to agglomerate fine ink particles released by floatation and can give reclaimed waste paper of a high whiteness by using a specified polymerized fatty acid ester. CONSTITUTION:A deinking agent for wastepaper is obtained by using at least one polymerized fatty acid ester of the formula (wherein x is 0, 1 or 2; y is 1, 2 or 3; x+y=2 or 3; n is 0-25; m is 10-80; D is a 20-30 C alkyl or alkenyl; EO is an ethylene oxide residue; and PO is a propylene oxide residue). In this way, a deinking agent which has an excellent ability to release an ink from waste paper and a high ability to agglomerate fine ink particles released by floatation and can give a reclaimed waste paper of a high whiteness can be obtained.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、新関、雑誌9,書物等の古紙から再生バルブ
をフローテーシッン法によって脱インキする場合、高白
免度の脱墨パルブを得るための脱墨用脱墨剤及びこれを
用いる脱墨方法に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention provides a method for obtaining deinked pulp with high brightness when deinking recycled valves from used paper such as Shinkansen, magazines 9, books, etc. by the floatation method. The present invention relates to a deinking agent for deinking and a deinking method using the same.

〔従来の技術及び問題点〕[Conventional technology and problems]

古紙を脱インキ薬品により処理して脱インキを行う方法
として次のこεが知られている.古紙を二一グーで微粉
砕した後又は微粉砕時に、水酸化アルカリ、過酸化水素
等の漂白剤、pH緩衝剤兼キレート剤としてケd酸ソー
ダ及び界面活性剤等より成る脱インキ薬品を用い悪。こ
の際バルブからインキの脱離を効率的に行うため説イン
キ剤(脱墨剤)としてポリオキシアルキ1/ンアルキル
エーテル、ポリオキシアルキレンアルキルフ五ノールエ
ーテルの如きノニオン界面活性剤を中心L、し、これら
にオレイン酸石鹸、高級アルコール硫酸エステル塩、α
−オレフィンスルホネートの如きアニオン系を組合せた
ものを相いる。モして室温から6 0=7 O℃で攪拌
下に数時間以内6こ保ち、バルブに付着したインキをは
<離する。この脱インキ工程を効率的に行うために、バ
ルブ濃度をめ来るだけ高くし、パルブ同志の機械的接触
で脱インキをはかることも知られでいる(公開56−6
3089). 次に、バルブ溶液を濃度1%前後に稀釈し、フローテー
ションを行う。その際バルブから脱離したインキや填料
・顔料等は空気泡に連行され系から除かれる。
The following method is known for deinking waste paper by treating it with deinking chemicals. After or at the time of finely pulverizing waste paper with 21 Gu, deinking chemicals consisting of bleaching agents such as alkali hydroxide and hydrogen peroxide, sodium chloride acid and surfactants as pH buffering agents and chelating agents are used. evil. At this time, in order to efficiently remove the ink from the valve, nonionic surfactants such as polyoxyalkylene alkyl ether and polyoxyalkylene alkyl pentol ether are used as the ink agent (deinking agent). These include oleic acid soap, higher alcohol sulfate salts, α
- Compatible with combinations of anionic systems such as olefin sulfonates. The ink was then kept at room temperature to 60=70°C under stirring for several hours to remove the ink adhering to the valve. In order to efficiently perform this deinking process, it is known that the concentration of the valves is increased as much as possible, and deinking is achieved through mechanical contact between the valves (Publication No. 56-6
3089). Next, the bulb solution is diluted to a concentration of around 1% and flotation is performed. At this time, the ink, filler, pigment, etc. that are released from the valve are entrained by air bubbles and removed from the system.

フローテーシッンを効率的に行う番;=は、離解時に分
離生威した微粒子のペンキを凝集させゐためにオレイン
酸やステアリン酸等の高級脂肪酸、パンオイル、々ロシ
ン等が使用されている(新聞(古紙)の流通・貯蔵段階
における繊維強度及び脱イン牛性の変化に関する調査報
告書、S760。3クリーンジャパンセンター).金属
石鹸不溶化物がフロック化し,その際にインキや顔料が
取り迭まれ、それらは気泡と共に系外に除かれる。非イ
オン系界面活性剤のみではインキ粒子が小さ《、フロン
ク形或時隨き6こくいが、詣肪酸等系又はその石鹸を用
いると凝集したインキ粒子は大きくなり、フローテーシ
ジン効果が太き《なる。脂肪酸の中でもオレイン酸(C
MC刊二紙薬品ε紙用機能材料p.36)ステアリン酸
、パルaチン酸が効果的である。脂肪酸は遊離状態又は
その石鹸の形で投入する.遊離状態で投入する場合は離
解時に投入したアルカリによって石鹸として機能する。
To efficiently carry out floatation, higher fatty acids such as oleic acid and stearic acid, bread oil, and rosin are used to coagulate the fine particles of paint separated during disintegration (newspaper). Investigation report on changes in fiber strength and de-ined beef quality during the distribution and storage stages of waste paper (S760.3 Clean Japan Center). The insolubilized metal soap becomes a floc, and at this time, the ink and pigment are removed and removed from the system along with air bubbles. If only a nonionic surfactant is used, the ink particles will be small (Fronck type or sometimes 6000 yen), but if a phosphorus fatty acid type or its soap is used, the aggregated ink particles will become larger, and the floatation effect will become larger. It becomes. Among fatty acids, oleic acid (C
MC Kanshi Paper Yakuhin ε Functional Materials for Paper p. 36) Stearic acid and palic acid are effective. Fatty acids are introduced in the free state or in the form of their soaps. When it is added in its free state, it functions as a soap due to the alkali added during disintegration.

胞肪酸の場合は液状のオレイン酸が作業性が良く効果も
大きいので最もよく使用されている。オ1/イン酸はイ
ンキに対する凝集力は高くフ0−テーシッン時に脱イン
キを効率的に行うことが出来る。しかし、オレイン酸を
用いると泡立ちが悪く、かつ凝集浮上したインキ部分の
フロックと泡乙の親和性も悪く、フ0−テーション装置
から分離したインキフロックが装置の配管系に付着した
りし、これが一度に流出したりし、工程上のトラブルの
原因になることがあった. 又、ステアリン酸やバルミチン酸は石ケンとして使用し
ようとすると水への溶解度が低いため、新たな溶解設備
が必要という不便さがあり、インキの凝集力が高く鮨肪
酸の中では低価格というメリットがあるにもかかわらず
、使いすらいという欠点があった. 一方、最近の古紙は、印刷物の多様化二−ズに対応して
印刷技術及び印刷インキの多様化のために、回収される
古紙の中には脱インキしにくい印刷物の混入率が増加し
たり、新開紙も凸版印刷からオフセット印刷へ移行し7
つつあり、インキ中の樹脂成分も多くなり回収新聞の脱
インキが困難になりつつある。こうした背景の下に数年
前がら多くの研究がなされ、特許の出瀬がなされている
。
In the case of fatty acids, liquid oleic acid is the most commonly used because it is easy to work with and has great effects. O1/inic acid has a high cohesive force against ink and can efficiently remove ink during printing. However, when oleic acid is used, foaming is poor, and the flocs in the coagulated and floated part of the ink have poor affinity with the foam. Sometimes they leaked out all at once, causing problems in the process. In addition, when trying to use stearic acid and valmitic acid as soap, they have low solubility in water, which inconveniences the need for new dissolving equipment.However, stearic acid and valmitic acid have a high cohesive force in ink, and are relatively inexpensive compared to sushi fatty acids. Despite its advantages, it had the disadvantage of being difficult to use. On the other hand, recently, due to the diversification of printing technology and printing ink in response to the diversification needs of printed materials, the proportion of printed materials that are difficult to deink has increased in the recovered waste paper. , Shinkaishi also transitioned from letterpress printing to offset printing.7
As the number of resin components in the ink increases, it is becoming difficult to remove ink from recovered newspapers. Against this background, much research has been carried out over the past few years, and patents have been issued.

例えばポリオキシアルキレンアルキルエーテル、ポリオ
キシアルキレンアル牛ルフ五ノールエーテルの如きノニ
オン界面活性剤を中心薬剤とし、これに泡立ち向」ニな
いし泡立ち調整剤として、アルキルサルフェート、アル
キルスルホナートを加え、更に前述した如く古紙からR
aしたインキの凝集剤εして脂肪酸を組み合わせた使わ
れ方が推奨されている。それでも十分に目的の脱インキ
性が難しくこれを解決せんと特にノニオン界面活性剤に
ついては各種の化合物が特許で提案されている。
For example, a nonionic surfactant such as polyoxyalkylene alkyl ether or polyoxyalkylene alkyl ether is used as the main agent, and an alkyl sulfate or alkyl sulfonate is added as a foaming agent or a foaming regulator. R from old paper
It is recommended to use a combination of a flocculant ε and a fatty acid in the ink. Even so, it is difficult to achieve the desired deinking property, and in order to solve this problem, various compounds have been proposed in patents, especially regarding nonionic surfactants.

その一例としてポリグリコール型のインキ溶出型脱墨剤
が提案され、電子コピー古紙の脱インキや工場実験が行
われかなりの改善がはかられたく静岡県製紙工業試験場
報告&4 0 ’88.12月)。
As an example, a polyglycol-type ink-eluting deinking agent was proposed, and a factory experiment was conducted to remove ink from used paper for electronic copying, and considerable improvements were expected.Report from the Shizuoka Prefecture Paper Industry Experiment Station &40'88.12 ).

〔問題点を解決するための手段〕[Means for solving problems]

そこで本発明者等は上記の問題点、すなわち古紙からの
インキの離脱力に優れ、かつフローテーションで離脱し
た微細なインキ粒子の凝集力が大きくて、高白色度の再
生古紙を得ることが出来る脱墨剤を開発すべく鋭意研究
した結果、本発明を完威した。
Therefore, the present inventors have solved the above problems, that is, it is possible to obtain recycled waste paper with excellent ink separation force from waste paper, high cohesive force of fine ink particles separated by flotation, and high whiteness. As a result of intensive research to develop a deinking agent, the present invention was successfully completed.

1分子中にアニオンとノニオンを同時に持つ化合物すな
わち重合脂肪酸に、部分的に脂肪酸基を残しながら、カ
ルボキシル基の一部をボリオキシエチレンやボリオキシ
エチレン・ボリオキシプロピレンの親水基を結合させた
ものを用いると脱墨効果が著しいことを見出し、本発明
を完威させた。
A compound that has both an anion and a nonion in one molecule, i.e., a polymerized fatty acid, in which some of the carboxyl groups are bonded to the hydrophilic groups of polyoxyethylene, polyoxyethylene, and polyoxypropylene, while leaving some fatty acid groups. It was discovered that the deinking effect was remarkable when using the above method, and the present invention was completed.

すなわち本発明は下記一般式(1)で表わすことができ
る。
That is, the present invention can be represented by the following general formula (1).

(但しXは0,1又は2、yは1,2又は3でかつx+
yは2又は3、mは0又は25以下の正の数、mは10
ないし80の正の数、Dは炭素数が20ないし36のア
ルキル基又はアルケニル基、EOはエチレンオキシド残
基、POはプロピレンオキシド残基) 重合脂肪酸エステル及びこれを少くとも一種含有する古
紙の脱墨剤ならびに該脱墨剤を用いる古紙の脱墨方法に
関する. 重合脂肪酸は天然物から合威して得られる混合物で充分
である.混合物はモノマー酸2〜70%、ダイマー酸3
0〜95%、トリマー酸2〜70%ベ生成物が固くなる
ので、トリマー酸リッチの場合よりダイマー酸リッチの
方が望ましい。脱インキ性能はいずれも大差はない. 重合脂肪酸とポリオキシアルキレンとの反応モル比は3
:lから1:2の範囲が望ましい。重合脂肪酸もポリオ
キシアルキレンも混合物であるから、その平均分子量で
みる.重合脂肪酸のモル比が多いと1分子中にの官能基
のモル数ではカルボキシル基〉ポリオキシアルキレン基
となり、全体としてみれば、アニオン性界面活性剤であ
る.一方逆になると重合脂肪酸のカルボキシル基のすべ
てがポリアルキレンオキシド基にふさがれるので、全体
としてノニオン界面活性剤となる.各種の割合で検討し
たところ、ほぼ当モルで構或するアニオン〜ノ二オン構
或脂肪酸が、最もよい結果を示した。
(However, X is 0, 1 or 2, y is 1, 2 or 3, and x+
y is 2 or 3, m is 0 or a positive number less than or equal to 25, m is 10
(Positive number from 80 to 80, D is an alkyl or alkenyl group having 20 to 36 carbon atoms, EO is an ethylene oxide residue, PO is a propylene oxide residue) Deinking of polymerized fatty acid esters and used paper containing at least one of them This paper relates to a deinking agent and a method for deinking waste paper using the deinking agent. A mixture obtained by synthesis of natural products is sufficient as the polymerized fatty acid. The mixture is 2% to 70% monomer acid, 3% dimer acid.
0-95% trimer acid, 2-70% trimer acid. Dimer acid rich is preferable to trimer acid rich because the product becomes hard. There is no significant difference in deinking performance. The reaction molar ratio of polymerized fatty acid and polyoxyalkylene is 3
A range of :1 to 1:2 is desirable. Both polymerized fatty acids and polyoxyalkylenes are mixtures, so look at their average molecular weights. When the molar ratio of polymerized fatty acids is high, the number of moles of functional groups in one molecule is carboxyl group > polyoxyalkylene group, and the surfactant is an anionic surfactant as a whole. On the other hand, in the reverse case, all of the carboxyl groups of the polymerized fatty acid are blocked by polyalkylene oxide groups, so the entire product becomes a nonionic surfactant. When various ratios were investigated, fatty acids having an anionic to nonionic structure in approximately equimolar proportions showed the best results.

脱墨剤として(1)式の化合物を使う場合、カセイソー
ダ、ケイ酸ソーダ、炭酸ソーダ、漂白剤等を添加する離
解時に混合使用する. 又、化合物(1)は遊離の型でも使えるが、アルカリ金
属塩、アンモニウム塩、アξン塩の水溶液として前もっ
て溶解してから使用してもよい。トリマーリッチのもの
を原料とすると塩としての水ヘの溶解度は低下する。遊
離の型で使う場合は加温し、溶液とするか、水、アルコ
ール、ケトン、芳香族炭化水素、脂肪族炭化水素、液体
脂肪酸、その他の良溶媒に溶解してハンドリングを改善
して使用するとよい.又、HLBが5〜15位の界面活
性剤を化合物(1)に対し5〜30%加え、水を加えて
乳化ないし溶解した形で用いることも出来る。
When using the compound of formula (1) as a deinking agent, it is mixed and used during disintegration when caustic soda, sodium silicate, soda carbonate, bleach, etc. are added. Compound (1) can be used in its free form, but it may also be used after being dissolved in advance as an aqueous solution of an alkali metal salt, ammonium salt, or ammonium salt. If a trimer-rich material is used as a raw material, the solubility of the salt in water will decrease. When used in free form, it can be heated to form a solution, or dissolved in water, alcohol, ketones, aromatic hydrocarbons, aliphatic hydrocarbons, liquid fatty acids, or other good solvents to improve handling. good. Alternatively, a surfactant having an HLB of 5 to 15 may be added to Compound (1) in an amount of 5 to 30%, and water may be added to emulsify or dissolve it.

化合物(1)は単独で用いてもよいが、他の界面活性剤
と組合わせて用いることが出来る。
Compound (1) may be used alone or in combination with other surfactants.

実施例にはヒマシ油構威脂肪酸であるリシノール酸との
組合せを中心として示したが、これに限定されるもので
はない。他の脂肪酸やポリアルキレンアルキルエーテル
、ポリオキシアルキレンアルキルフェノールエーテル、
アルキルサルフェート、アルキルスルホネート等と併用
するとフローテーシッン効果が向上し、より白色度の高
い回収古紙を得ることが出来る.混合割合は特に規定す
るものではないが、離解時に加えるアニオン、ノニオン
の種類、pH、温度、脱墨装置、古紙の種類等によって
個々泡立ち量等異なるので、適切な配合割合を選定する
とよい。
Although the examples mainly show combinations of castor oil with ricinoleic acid, which is a fatty acid, the present invention is not limited to this. Other fatty acids, polyalkylene alkyl ethers, polyoxyalkylene alkylphenol ethers,
When used in combination with alkyl sulfates, alkyl sulfonates, etc., the floatation effect is improved and recovered waste paper with higher whiteness can be obtained. Although the mixing ratio is not particularly specified, the amount of foaming varies depending on the type of anion and nonion added during disintegration, pH, temperature, deinking equipment, type of waste paper, etc., so it is recommended to select an appropriate mixing ratio.

化合物(1)の添加璽は古紙の種類、脱墨設備の違い、
併用する界面活性剤の種類等によって違うが、ドライ古
紙当り0.01〜1.Owt%である。
The addition of compound (1) depends on the type of waste paper, the deinking equipment,
Although it varies depending on the type of surfactant used in combination, it is 0.01 to 1.0% per dry waste paper. Owt%.

以下に実施例によって説明するが、本発明はこれらに限
定されるものではない。
Examples will be described below, but the present invention is not limited thereto.

ダイマー酸エステル合威実施例 犬見班土一 酸価194、ケン化価198、平均分子量599でモノ
マー酸8%、ダイマー酸74%、トリマー酸18%から
なる重合脂肪酸36グラム(0.06モル)と平均分子
量2000のボリオキシエチレングリコール60グラム
(0.03モル)及ヒトルエン50−1を加え、p一ト
ルエンスルホン酸180gを触媒とし、170℃で、0
.06モルの水が出るまで約50分間加熱環流した.■
00℃まで冷却後p一トルエンスルホン酸ソーダを当モ
ルの重曹0.442grを加え、触媒を中和する.その
後減圧下で40℃から80℃に昇温しつつ約1hr(す
て かlトルエン臭がなくなるまで脱トルエンし、酸価34
の重合脂肪酸とポリオ・キシヱチレングリコールのモル
比が2=1のエステルを得た。
Example of synthesis of dimer acid ester Inumibanto 36 grams (0.06 mol) of a polymerized fatty acid consisting of 8% monomer acid, 74% dimer acid, and 18% trimer acid with a monoacid value of 194, a saponification value of 198, and an average molecular weight of 599. ), 60 g (0.03 mol) of polyoxyethylene glycol with an average molecular weight of 2000, and 50-1 mol of hydroxyethylene glycol, and using 180 g of p-toluenesulfonic acid as a catalyst, the mixture was heated at 170°C to 0.
.. The mixture was heated and refluxed for about 50 minutes until 0.6 moles of water came out. ■
After cooling to 00°C, add 0.442g of sodium bicarbonate equivalent to 0.442g of sodium p-toluenesulfonate to neutralize the catalyst. Thereafter, the temperature was raised from 40°C to 80°C under reduced pressure for about 1 hr (toluene was removed until the toluene odor disappeared, and the acid value was 34.
An ester with a molar ratio of polymerized fatty acid and polyoxyethylene glycol of 2=1 was obtained.

実益拠L= 実施例1と同一の重合脂肪酸30グラム(0.05モル
)と平均分子量2千のポリオキシェチ【,・ングリコー
ル100グラム(0.05モル〉を用い、実施例1と同
様に反応した。 170℃で0.05モルの水が出るま
で約35分間加熱環流した。反応終了後は実施例1と同
様に後恕理し、酸価21の乗合脂肪酸とポリオキシエチ
レンの1:1モル比のエステルを得た。
Practical basis L = Reaction was carried out in the same manner as in Example 1 using 30 grams (0.05 mol) of the same polymerized fatty acid as in Example 1 and 100 grams (0.05 mol) of polyoxyethylene glycol having an average molecular weight of 2,000. The mixture was heated and refluxed at 170°C for about 35 minutes until 0.05 mol of water was released. After the reaction was completed, the mixture was treated in the same manner as in Example 1, and a 1:1 combination of a hybrid fatty acid with an acid value of 21 and polyoxyethylene was carried out. A molar ratio of esters was obtained.

実一施潰1一 実施例1と同一の重合脂肪酸15グラム(0.025モ
ル)と平均分子量2千のボリオキシエチレングリコール
100g(0.05モル)を用い、実施例1ε同様に反
応した.170℃で0.05モルの水が出るまで約60
分間加熱環流した。反応終了後は実施例1と同様に後処
理し、酸価4の重合脂肪酸とポリオキシェヂレンのモル
比が1:2のエステルを得た。
Example 1 Crushed 11 A reaction was carried out in the same manner as in Example 1ε using 15 g (0.025 mol) of the same polymerized fatty acid as in Example 1 and 100 g (0.05 mol) of polyoxyethylene glycol having an average molecular weight of 2,000. Approximately 60 minutes until 0.05 mol of water comes out at 170℃
The mixture was heated to reflux for a minute. After the reaction was completed, post-treatment was carried out in the same manner as in Example 1 to obtain an ester having a molar ratio of polymerized fatty acid having an acid value of 4 to polyoxyethylene in a molar ratio of 1:2.

大旌槻土一 実施例lと同一の重合脂肪酸30グラム(0.05モル
)と平均分子!2 2 4 0のポリオキシェチンボリ
オキシプロピレングリコール(エチレンオキサイドとプ
ロピレンオキサイドの重合度はそれぞれ45モル及び4
モル〉 i12グラム(0.05モル)を用いた以外は
実施例2と同様に反応、後処理を行い、酸価l9の重合
脂肪酸とボリオキシエチレンボリオキプロピレングリコ
ールの1:1モル比のエステルを得た。
30 grams (0.05 mol) of the same polymerized fatty acid as in Example 1 and the average molecule! 2 2 4 0 polyoxyethine polyoxypropylene glycol (the degree of polymerization of ethylene oxide and propylene oxide is 45 mol and 4 mol, respectively)
mol> The reaction and post-treatment were carried out in the same manner as in Example 2 except that 12 grams (0.05 mol) of i was used, and an ester of polymerized fatty acid with an acid value of 19 and bolyoxyethylene borioquipropylene glycol in a 1:1 molar ratio was prepared. I got it.

〔実施例5〜21〕 基本的にはJapan TAPPI llh39−82
にIll若干の変更の下に実施した. 古紙は東京都内で発行後3カ月経過した朝日新聞を使用
した. 1800a+j!の50℃強の温水に乾燥古紙に対しカ
セイソーダ1. 5%、3号ケイ酸ソーダ3.0%、脱
墨剤として化合物(1》と表に示すその他の脱墨助剤の
所定量及び30%過酸化水素水1.0%び及シュレッグ
ーで粉砕した古新聞75gを東洋テスター■製の標準離
解機に入れ、50℃、lO分間離解する。その後50℃
、60分間静置保温後、5分間同様に離解機中で離解す
る。
[Examples 5 to 21] Basically Japan TAPPI llh39-82
This was implemented with some changes. The used paper used was Asahi Shimbun, which was published in Tokyo for three months. 1800a+j! 1. Caustic soda for dried waste paper in hot water of just over 50℃. 5%, No. 3 sodium silicate 3.0%, specified amounts of compound (1) as a deinking agent and other deinking aids shown in the table, 1.0% of 30% hydrogen peroxide solution, and pulverized with Schlegoo. Put 75g of old newspapers into a standard disintegrator manufactured by Toyo Tester ■ and disintegrate them at 50°C for 10 minutes.
After being left to stand and warm for 60 minutes, it is similarly disintegrated in a disintegrator for 5 minutes.

離解液1)50gを採り、水で稀釈し、バルプ濃度1パ
ルブに稀釈し、34〜36℃に設定し、熊谷理機■製の
フローテーターにて10分間フローテーションする。
1) Take 50 g of the disintegrating solution, dilute it with water, dilute it to a pulp concentration of 1 pulse, set the temperature to 34-36°C, and float it for 10 minutes using a floatator manufactured by Kumagai Riki ■.

空気送入開始前の攪拌時に塩化カルシウムを38ppl
1?!度になるように加えるや フローテーシジンの途中、3分、7分、10分時に泡を
除去しつつ、フローテーシジン間に流出した泡液量及び
泡高さ、泡色の経時変化を追跡する.フローテーション
終了後1.Olをとり60メッシュふるい上でしぼり、
約90〜95gとし、炉液で稀釈して、100gとし、
水で稀釈し1.Olに戻す。
Add 38 ppl of calcium chloride during stirring before starting air supply.
1? ! While adding the foam to a certain degree and removing the foam at 3, 7, and 10 minutes during the flow test, track the amount of foam flowing out during the flow test, as well as changes in foam height and foam color over time. do. After flotation 1. Take the ol and squeeze it on a 60 mesh sieve,
About 90 to 95 g, diluted with furnace liquid to make 100 g,
Dilute with water 1. Return to Ol.

古紙3.0gに担当する離解液、フローテーション終了
液及び仕上げ液それぞれを均一に採液し.JIS P 
8209に従い試験用手すき祇を調製した。白色度はハ
ンター白色度JIS P 8123によって測定した。
Dissolve the disintegration liquid, flotation completion liquid, and finishing liquid uniformly on 3.0 g of waste paper. JIS P
8209 was prepared for the test. The whiteness was measured according to Hunter Whiteness JIS P 8123.

各実施例の結果を表1に示した.表1中の化合物1のD
A,DBは重合脂肪酸の略号で、表の(注)に示した組
戒を持つ,DA− (RO) ,,DAはDAと(RO
).のモル比が2:lのもの、DA− (RO),はモ
ル比が1:1のもの、(R○) ,l−DA− (RO
).はDAと(RO),1のモル比が1:2で合威した
ものを意味する.Rはエチレンやプロピレンを表わす.
以下に実施例の内容について説明する. 比較例(1) (2)の如くC.の脂肪酸にエチレンオ
キサイドを付加したノニオン界面活性剤はフローテーシ
gン時に泡立ちもほとんどなく、フローテーションでの
脱インキ効果(フローテーシッン後の白色度(bl一離
解後の白色度(a)一効果(l))は0.1〜0.2と
小さくほとんど脱インキ効果は認められなかった。一方
これらのノ二オン界面活性とC.脂肪酸相当の分子量と
ボリオキシエチレンの分子量の割合が同一の実施例l1
の化合物では流出泡液量も1).7%と大きくなり、フ
ローテーシッンでの脱インキ効果も0.1〜0.2から
3.9に上昇し、重合脂肪酸を親油基とするものは大き
な脱インキ効果を認めた. 9 実施例5.6.7及び8,9,1/はダイマー酸とポリ
オキシエチレンのモル比を2:1.1:1,1)の割合
のもので、通常の界面活性剤の分類に従えば、それぞれ
アニオン、アニオン・ノニオン、ノニオンに分類される
もので、これらとリシノール酸とを併用した例である。
The results of each example are shown in Table 1. D of compound 1 in Table 1
A and DB are abbreviations for polymerized fatty acids, and have the combination shown in the note in the table.
). , with a molar ratio of 2:l, DA- (RO), with a molar ratio of 1:1, (R○),l-DA- (RO
). means that DA and (RO) are combined in a molar ratio of 1:2. R represents ethylene or propylene.
The contents of the example are explained below. As in Comparative Examples (1) and (2), C.I. The nonionic surfactant, which is made by adding ethylene oxide to the fatty acid of )) was as small as 0.1 to 0.2, and almost no deinking effect was observed.On the other hand, these nonionic surfactants and C. Examples in which the ratio of the molecular weight equivalent to fatty acid and the molecular weight of polyoxyethylene were the same l1
For the compound, the amount of foam flowing out is also 1). 7%, and the deinking effect with floatation also increased from 0.1 to 0.2 to 3.9, and a large deinking effect was observed with polymerized fatty acids as lipophilic groups. 9 Examples 5.6.7 and 8,9,1/ have a molar ratio of dimer acid and polyoxyethylene of 2:1.1:1.1), and are classified as ordinary surfactants. Accordingly, they are classified into anion, anion/nonion, and nonion, respectively, and this is an example of using these together with ricinoleic acid.

この中ではアニオン・ノニオン型が優れていた。Among these, the anionic and nonionic types were superior.

Claims (3)

【特許請求の範囲】[Claims] (1)下記一般式( I ) ▲数式、化学式、表等があります▼( I ) (但しxは0、1又は2、yは1、2又は3でかつx+
yは2又は3、mは0又は25以下の正の数、mは10
ないし80の正の数、Dは炭素数が20ないし36のア
ルキル基又はアルケニル基、EOはエチレンオキシド残
基、POはプロピレンオキシド残基) で表わされる重合脂肪酸エステル。
(1) The following general formula (I) ▲There are mathematical formulas, chemical formulas, tables, etc.▼(I) (However, x is 0, 1 or 2, y is 1, 2 or 3, and x +
y is 2 or 3, m is 0 or a positive number less than or equal to 25, m is 10
A positive number from 80 to 80, D is an alkyl group or alkenyl group having 20 to 36 carbon atoms, EO is an ethylene oxide residue, and PO is a propylene oxide residue).
(2)下記一般式( I ) ▲数式、化学式、表等があります▼( I ) (但しxは0、1又は2、yは1、2又は3でかつx+
yは2又は3、mは0又は25以下の正の数、mは10
ないし80の正の数、Dは炭素数が20ないし36のア
ルキル基又はアルケニル基、EOはエチレンオキシド残
基、POはプロピレンオキシド残基) で表わされる重合脂肪酸エステルを少くとも一種含有す
ることを特徴とする古紙の脱墨剤。
(2) The following general formula (I) ▲There are mathematical formulas, chemical formulas, tables, etc.▼(I) (However, x is 0, 1 or 2, y is 1, 2 or 3, and x +
y is 2 or 3, m is 0 or a positive number less than or equal to 25, m is 10
D is an alkyl group or alkenyl group having 20 to 36 carbon atoms, EO is an ethylene oxide residue, and PO is a propylene oxide residue). A deinking agent for used paper.
(3)古紙を脱インキ薬品を用いて脱インキを行う工程
に於て、脱インキ剤として下記一般式( I )▲数式、
化学式、表等があります▼( I ) (但しxは0、1又は2、yは1、2又は3でかつx+
yは2又は3、mは0又は25以下の正の数、mは10
ないし80の正の数、Dは炭素数が20ないし36のア
ルキル基又はアルケニル基、EOはエチレンオキシド残
基、POはプロピレンオキシド残基) で表わされる重合脂肪酸エステルを少くとも一種含有す
る古紙の脱墨剤を用いることを特徴とする古紙の脱墨方
法。
(3) In the process of deinking waste paper using a deinking chemical, the following general formula (I) ▲ mathematical formula,
There are chemical formulas, tables, etc.▼(I) (However, x is 0, 1 or 2, y is 1, 2 or 3, and x+
y is 2 or 3, m is 0 or a positive number less than or equal to 25, m is 10
A positive number from 80 to 80, D is an alkyl group or alkenyl group having 20 to 36 carbon atoms, EO is an ethylene oxide residue, and PO is a propylene oxide residue). A method for deinking waste paper, which is characterized by using an ink agent.
JP1159038A 1989-06-21 1989-06-21 Polymerized fatty acid ester and deinking of waste-paper by using same Pending JPH0324126A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1159038A JPH0324126A (en) 1989-06-21 1989-06-21 Polymerized fatty acid ester and deinking of waste-paper by using same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1159038A JPH0324126A (en) 1989-06-21 1989-06-21 Polymerized fatty acid ester and deinking of waste-paper by using same

Publications (1)

Publication Number Publication Date
JPH0324126A true JPH0324126A (en) 1991-02-01

Family

ID=15684887

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1159038A Pending JPH0324126A (en) 1989-06-21 1989-06-21 Polymerized fatty acid ester and deinking of waste-paper by using same

Country Status (1)

Country Link
JP (1) JPH0324126A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03193986A (en) * 1989-12-22 1991-08-23 Harima Chem Inc Deinking agent for reclaiming waste paper
FR2674871A1 (en) * 1989-10-26 1992-10-09 Harima Chemicals Inc DEINKING AGENT FOR THE REGENERATION OF OLD PRINTED PAPERS.
US5880077A (en) * 1997-08-29 1999-03-09 High Point Chemical Corporation Wastepaper reclaiming deinking agent
JP2024159222A (en) * 2023-04-28 2024-11-08 築野グループ株式会社 Ester of dibasic acid and polyoxyalkylene glycol

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2674871A1 (en) * 1989-10-26 1992-10-09 Harima Chemicals Inc DEINKING AGENT FOR THE REGENERATION OF OLD PRINTED PAPERS.
JPH03193986A (en) * 1989-12-22 1991-08-23 Harima Chem Inc Deinking agent for reclaiming waste paper
US5880077A (en) * 1997-08-29 1999-03-09 High Point Chemical Corporation Wastepaper reclaiming deinking agent
JP2024159222A (en) * 2023-04-28 2024-11-08 築野グループ株式会社 Ester of dibasic acid and polyoxyalkylene glycol

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