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JP2810538B2 - Deinking agent for recycled paper - Google Patents
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JP2810538B2 - Deinking agent for recycled paper - Google Patents

Deinking agent for recycled paper

Info

Publication number
JP2810538B2
JP2810538B2 JP33446390A JP33446390A JP2810538B2 JP 2810538 B2 JP2810538 B2 JP 2810538B2 JP 33446390 A JP33446390 A JP 33446390A JP 33446390 A JP33446390 A JP 33446390A JP 2810538 B2 JP2810538 B2 JP 2810538B2
Authority
JP
Japan
Prior art keywords
ethylene oxide
propylene oxide
alcohol
compound
deinking agent
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 - Fee Related
Application number
JP33446390A
Other languages
Japanese (ja)
Other versions
JPH04202884A (en
Inventor
公司 浜口
英明 漆畑
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.)
Kao Corp
Original Assignee
Kao Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kao Corp filed Critical Kao Corp
Priority to JP33446390A priority Critical patent/JP2810538B2/en
Publication of JPH04202884A publication Critical patent/JPH04202884A/en
Application granted granted Critical
Publication of JP2810538B2 publication Critical patent/JP2810538B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/64Paper recycling

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  • Paper (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は新聞、雑誌等の古紙再生時に用いられる脱墨
剤に関する。更に詳しくは新聞、雑誌等をフロテーショ
ン法及びフロテーション/洗浄コンビネーションシステ
ムで脱墨処理を行うに際し高白色度のそして残インキ数
の少ない脱墨パルプを得る事の出来る脱墨剤に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a deinking agent used for recycling used paper such as newspapers and magazines. More specifically, the present invention relates to a deinking agent capable of obtaining a deinked pulp having high whiteness and a small number of remaining inks when performing deinking treatment on newspapers, magazines and the like by a flotation method and a flotation / washing combination system.

〔従来の技術及び発明が解決しようとする課題〕[Problems to be solved by conventional technology and invention]

新聞、雑誌等の再生利用は古くから行われて来ている
が、特に最近はパルプ資源の不足やその価格の高騰、更
にはゴミ対策、森林資源保護といった観点からもその有
効利用は益々重要性を帯びてきている。その強まるニー
ズに応えるように脱墨パルプの用途も高度利用技術開発
にも拍車がかかっている。一方、最近の古紙は印刷技
術、印刷方式の変化、印刷インキ成分の変化により脱墨
と云う点から見れば一層険しい状況になってきている。
Recycling of newspapers, magazines, etc. has been practiced for a long time, but in recent years, the effective use of pulp resources has become increasingly important from the viewpoint of shortage of pulp resources and soaring prices, as well as measures against garbage and protection of forest resources. It is taking on. In order to meet the growing needs, the use of deinked pulp and the development of advanced utilization technologies are being spurred. On the other hand, recently used paper has become even more rugged in terms of deinking due to changes in printing techniques, printing methods, and printing ink components.

そこで、より以上脱墨を促進させる為、装置へも改良
が加えられて来ている。例えば、タワーの設置による高
濃度熟成処理、物理力によってより一層インキ剥離を促
進させるためのディスパイザー、ニーダーの導入、更に
は高濃度離解パルパーの設置等が挙げられる。また、フ
ローテーターにおいても、高気泡型フローテーターの導
入が盛んになりつつある。
Therefore, in order to further promote deinking, improvements have been made to the apparatus. For example, high-concentration aging treatment by installing a tower, introduction of a dispenser and a kneader for further promoting ink peeling by physical force, and installation of a high-concentration disintegrating pulper are also included. In addition, the introduction of a high-bubble type floatator has also become active in floatators.

古紙からインキその他の不純物を分離除去する為従来
から用いられて来た薬剤としては、苛性ソーダ、珪酸ソ
ーダ、炭酸ソーダ、リン酸ソーダ等のアルカリ剤、過酸
化水素、次亜硫酸塩、次亜塩素酸塩等の漂白剤、EDTA、
DTPA等の金属イオン封鎖剤と共に、脱墨剤として、アル
キルベンゼンスルホン酸塩、高級アルコール硫酸エステ
ル塩、α−オレフィンスルホン酸塩、ジアルキルスルホ
サクシネート等の陰イオン活性剤、高級アルコール、ア
ルキルフェノール及び脂肪酸のエチレンオキシド付加
物、アルカノールアマイド類等の非イオン活性剤が単独
又は2種以上配合されて使用されて来た。しかしこれら
の脱墨剤ではフロテーション処理における起泡性は大き
いもののインキ捕集能が小さく、また、洗浄法において
もその洗浄力が弱いゆえ、低品質の脱墨パルプしか得ら
れなかった。更には、高白色度が得られたとしても、く
すみがあるため、脱墨パルプの用途制限(板紙の表下へ
の使用量減少、新聞紙への配合量減少等)や、くすみを
無くすため漂白剤使用量を増加せざるを得ないといった
状況であった。
Chemicals conventionally used to separate and remove ink and other impurities from waste paper include alkaline agents such as caustic soda, sodium silicate, sodium carbonate, and sodium phosphate, hydrogen peroxide, hyposulfite, and hypochlorous acid. Bleach such as salt, EDTA,
Along with sequestering agents such as DTPA, as deinking agents, anionic activators such as alkylbenzene sulfonates, higher alcohol sulfates, α-olefin sulfonates, dialkyl sulfosuccinates, higher alcohols, alkylphenols and fatty acids. Nonionic surfactants such as ethylene oxide adducts and alkanolamides have been used alone or in combination of two or more. However, these deinking agents have a high foaming property in the flotation treatment, but have a low ink collecting ability, and have a low detergency in the washing method, so that only low-quality deinked pulp can be obtained. Furthermore, even if a high whiteness is obtained, there is dullness, so the use of deinked pulp is restricted (reduction of the amount of paperboard used below and below, blending in newsprint, etc.) and bleaching to eliminate dullness. In this situation, the amount of the agent used had to be increased.

〔課題を解決するための手段〕[Means for solving the problem]

本発明者らは、フロテーション処理工程において優れ
たインキ捕集能を示し、高白色度、低残インキ数且つ未
剥離インキ数の少ない脱墨パルプを得ることのできる古
紙再生用脱墨剤を開発すべく鋭意研究を行なった結果、
本発明の完成するに至った。
The present inventors have developed a deinking agent for wastepaper recycling that exhibits excellent ink collecting ability in the flotation treatment process and can obtain deinked pulp having high whiteness, a low number of residual inks, and a small number of unstripped inks. As a result of intensive research to develop,
The present invention has been completed.

すなわち本発明は、下記(A),(B)又は(C)で
表されるOH基を含有する化合物とモノハロゲン低級カル
ボン酸塩との反応生成物を有効成分とする古紙再生用脱
墨剤を提供するものである。
That is, the present invention provides a deinking agent for recycling used paper, comprising, as an active ingredient, a reaction product of a compound containing an OH group represented by the following (A), (B) or (C) and a monohalogen lower carboxylate. Is provided.

(A); 炭素数5〜24のヒドロキシ脂肪酸にエチレンオキシド
とプロピレンオキシドとをエチレンオキシド/プロピレ
ンオキシド=1〜4(モル比)の割合となるように両者
合計で平均10〜50モル付加させた化合物 (B); エチレンオキシドとプロピレンオキシドとをエチレン
オキシド/プロピレンオキシド=1〜4(モル比)の割
合となるように両者合計でOH基1個当たり平均10〜50モ
ル付加させたアルコールと、炭素数5〜24のヒドロキシ
脂肪酸とのエステル化合物 (C); 炭素数5〜24のヒドロキシ脂肪酸とアルコールとのエ
ステルにエチレンオキシドとプロピレンオキシドとをエ
チレンオキシド/プロピレンオキシド=1〜4(モル
比)の割合となるように両者合計でOH基1個当たり平均
10〜50モル付加させた化合物 脱墨剤に必要な機能としては、 セルロース/インキ間の界面張力低下能 セルロースから剥離したインキの再付着防止性 気泡へのインキの吸着性が高いこと 適正な起泡性 の4つを挙げることができる。脱墨剤はこれら4つの機
能をバランスよく備えていなければならない。本発明の
古紙再生用脱墨剤は上記のに優れ、未剥離インキ数が
少ない脱墨パルプを得ることができる。
(A); a compound obtained by adding an average of 10 to 50 moles of ethylene oxide and propylene oxide to a hydroxy fatty acid having 5 to 24 carbon atoms in a ratio of ethylene oxide / propylene oxide = 1 to 4 (molar ratio) in total. B) an alcohol in which ethylene oxide and propylene oxide are added in an average of 10 to 50 mol per OH group so that the ratio of ethylene oxide / propylene oxide is 1 to 4 (molar ratio); Ester compound with 24 hydroxy fatty acids (C); an ester of a hydroxy fatty acid having 5 to 24 carbon atoms and an alcohol, wherein ethylene oxide and propylene oxide are in a ratio of ethylene oxide / propylene oxide = 1 to 4 (molar ratio). Average for each OH group in total
Compounds with 10 to 50 moles added The functions required for the deinking agent include the ability to lower the interfacial tension between cellulose and ink. The ability to prevent redeposition of ink peeled from cellulose. The high adsorption of ink to air bubbles. And four types of foam. A deinking agent must have these four functions in a well-balanced manner. The deinking agent for recycling waste paper of the present invention is excellent in the above, and can obtain deinked pulp having a small number of unstripped ink.

本発明において(A),(B)又は(C)の化合物を
得るために用いられるOH基含有化合物に付加させるエチ
レンオキシド及びプロピレンオキシドはブロック又はラ
ンダム付加のいずれでもよいが、好ましくはランダム付
加である。エチレンオキシドとプロピレンオキシドのモ
ル比はエチレンオキシド/プロピレンオキシド=1〜4
の範囲が良く、好ましくは1〜3の範囲である。このモ
ル比が1より小さい場合、セルロースから離脱したイン
キの分散力が大きく、更にフロテーター液面上での泡沫
層形成能力が弱いため、インキを保持した泡沫層が少な
くなる。その結果、白色度が低くなる。逆にモル比が4
より大きい場合、フロテーター中での気泡吸着性が小さ
く、その結果、泡沫層色相もインキ捕集性が低いことを
示し白っぽくなる。更にフロテーター液面上での泡沫層
形成能力が強いためフロスの泡量が多い。また、フロス
ピットでの破泡性が悪いといった操業性にとって極めて
問題のある現象が多発する。
In the present invention, ethylene oxide and propylene oxide added to the OH group-containing compound used for obtaining the compound (A), (B) or (C) may be either block or random addition, but is preferably random addition. . The molar ratio of ethylene oxide to propylene oxide is ethylene oxide / propylene oxide = 1 to 4.
Is good, and preferably is in the range of 1-3. When the molar ratio is less than 1, the dispersing power of the ink detached from the cellulose is large, and the ability of forming a foam layer on the liquid level of the flotator is weak, so that the number of foam layers holding the ink is reduced. As a result, the whiteness decreases. Conversely, if the molar ratio is 4
If it is larger, the air bubble adsorbing property in the flotator is low, and as a result, the hue of the foam layer becomes whitish, indicating that the ink collecting property is low. Further, since the foam layer has a strong ability to form a foam layer on the liquid level of the flotator, the amount of froth foam is large. In addition, phenomena that are extremely problematic for operability, such as poor foaming properties in the frost pit, frequently occur.

エチレンオキシドとプロピレンオキシドの付加モル数
は1活性水素原子に対して合計して平均10〜50モルがよ
い。好ましくは20〜35モルである。付加モル数が10より
小さい場合、セルロースからのインキ剥離性及びセルロ
ースから離脱したインキの捕集性が小さいため、白色度
が低くなる。また、付加モル数が50より大きい場合、フ
ロテーター液面上での泡沫層形成能力が弱くなるためイ
ンキを捕集した泡沫層が系外に除去されず、その結果と
して白色度が低くなるといった欠点を有する。
The number of moles of ethylene oxide and propylene oxide added is preferably 10 to 50 moles on average per 1 active hydrogen atom. Preferably it is 20 to 35 mol. When the number of moles added is less than 10, the whiteness decreases because the ink releasability from cellulose and the ability to collect ink released from cellulose are small. On the other hand, if the number of added moles is larger than 50, the ability to form a foam layer on the flotator liquid surface is weakened, so that the foam layer that has collected the ink is not removed outside the system, and as a result, the whiteness is reduced. Having.

本発明に用いられる炭素数5〜24のヒドロキシ脂肪酸
としては、12−ヒドロキシステアリン酸、2−ヒドロキ
シベヘン酸、2−ヒドロキシウンデカン酸、ジ−3−ヒ
ドロキシラウリン酸、テトラ−3−ヒドロキシトリデカ
ン酸、12−オキシオレイン酸等が挙げられる。
Examples of the hydroxy fatty acid having 5 to 24 carbon atoms used in the present invention include 12-hydroxystearic acid, 2-hydroxybehenic acid, 2-hydroxyundecanoic acid, di-3-hydroxylauric acid, and tetra-3-hydroxytridecanoic acid , 12-oxyoleic acid and the like.

本発明において、ヒドロキシ脂肪酸と反応させるアル
コールとしては、炭素数1〜24の一価のアルキルもしく
はアルケニルアルコール又は多価アルコールが挙げられ
る。一価アルコールとしてはメタノール、エタノール等
の低級アルコールや、脂肪酸アルコール等の高級アルコ
ールが挙げられる。多価アルコールとしては、二価アル
コール或いは糖アルコールが好適に使用される。二価ア
ルコールとしてはエチレングリコール、プロピレングリ
コール、ブタンジオール等が挙げられる。また、糖アル
コールとしてはソルビトール、ペンタエリスリトール等
が挙げられる。これらの他に三価アルコールとしてグリ
セリン、トリメチロールプロパン等が挙げられる。本発
明においては炭素数5〜24のヒドロキシ脂肪酸とアルコ
ールとのエステルにはこれらを含有するひまし油、硬化
ひまし油等も含まれる。
In the present invention, examples of the alcohol to be reacted with the hydroxy fatty acid include a monovalent alkyl or alkenyl alcohol having 1 to 24 carbon atoms or a polyhydric alcohol. Examples of the monohydric alcohol include lower alcohols such as methanol and ethanol, and higher alcohols such as fatty acid alcohols. As the polyhydric alcohol, a dihydric alcohol or a sugar alcohol is preferably used. Examples of the dihydric alcohol include ethylene glycol, propylene glycol, butanediol, and the like. Examples of the sugar alcohol include sorbitol and pentaerythritol. In addition to these, glycerin, trimethylolpropane and the like can be mentioned as trihydric alcohols. In the present invention, the ester of a C5-24 hydroxy fatty acid and an alcohol includes castor oil and hardened castor oil containing these.

本発明において、上記化合物(A)〜(C)とモノハ
ロゲン低級カルボン酸塩の反応割合は、化合物(A)〜
(C)の残存OH基1個に対してモノハロゲン低級カルボ
ン酸塩を0.8〜1.2モル用いるのが好ましい。この仕込割
合に対して極端に(A),(B)又は(C)が多い場
合、フロテーターでのインキ補集能が小さくなるため白
色度が低くなる可能性がある。逆の場合、即ち極端にモ
ノハロゲン低級カルボン酸塩が多い場合はセルロースか
らのインキ剥離性が小さいため未剥離インキが多くな
り、見栄えの悪い脱墨パルプしか得られない。
In the present invention, the reaction ratio between the compounds (A) to (C) and the monohalogen lower carboxylate is determined by the ratio of the compounds (A) to
It is preferable to use 0.8 to 1.2 moles of the monohalogen lower carboxylate per one residual OH group of (C). If (A), (B) or (C) is extremely large with respect to this charging ratio, the whiteness may be reduced because the ink collecting ability in the rotator is reduced. In the opposite case, that is, when the amount of monohalogenated lower carboxylate is extremely large, the ink peeling property from cellulose is small, so that the amount of unstripped ink increases, and only deinked pulp with poor appearance can be obtained.

本発明に用いられるモノハロゲン低級カルボン酸塩と
しては、モノクロロ酢酸、モノブロム酢酸、モノクロロ
プロピオン酸、モノブロムプロピオン酸等のナトリウム
塩、カリウム塩等が挙げられる。
Examples of the monohalogenated lower carboxylate used in the present invention include sodium salts and potassium salts of monochloroacetic acid, monobromoacetic acid, monochloropropionic acid, monobromopropionic acid and the like.

本発明の古紙再生用脱墨剤の製造法は特に限定される
ものではなく、前記に記載の(A),(B)又は(C)
の如きOH基を有する化合物とモノハロゲン低級カルボン
酸塩とをアルカリ雰囲気下で混合加熱して反応させ、製
造することができる。例えば、特公昭54−4932号公報に
記載されている製造法が該当する。
The method for producing the deinking agent for recycling waste paper of the present invention is not particularly limited, and the method (A), (B) or (C) described above may be used.
And a monohalogenated lower carboxylate are mixed and heated and reacted in an alkaline atmosphere to produce the compound. For example, the production method described in JP-B-54-4932 corresponds to this.

本発明の古紙再生用脱墨剤は古紙離解工程、ニーダー
処理工程、熟成タワー工程及びフロテーション処理の何
れかもしくは各工程へ分割添加してもよいが、古紙離解
工程へ添加した場合が最も効果が高い。また、その添加
量は原料古紙に対して0.05〜1.0重量%が好ましい。
The deinking agent for recycling waste paper of the present invention may be added to any of the waste paper disintegration step, the kneader treatment step, the aging tower step and the flotation treatment or to each step, but the most effective is the case where it is added to the waste paper disintegration step. Is high. The amount of addition is preferably 0.05 to 1.0% by weight based on the raw waste paper.

また、本発明の古紙再生用脱墨剤は従来一般に用いら
れている公知の脱墨剤と併用することもできる。
Further, the deinking agent for reclaiming used paper of the present invention can be used in combination with a known deinking agent generally used conventionally.

〔実施例〕〔Example〕

以下実施例により本発明を具体的に説明するが、本発
明はこれらの実施例に限定されるものではない。
Hereinafter, the present invention will be described specifically with reference to Examples, but the present invention is not limited to these Examples.

製造例1 12−ヒドロシステアリン酸にエチレンオキシド(以下
EOと記す)20モル当量、プロピレンオキシド(以下POと
記す)10モル当量をブロック付加した化合物463.0gとモ
ノクロロ酢酸ナトリウム27.6gを攪拌棒、温度計、滴下
ロート及び冷却器付きクライゼン管を備えた4ツ口1
反応フラスコに仕込み、よく攪拌しながら反応温度80〜
85℃、50mm/Hgの減圧度に保ち、NaOH9.5gを48%水溶液
として1時間にわたって滴下する。この時留出する水は
冷却器により凝縮されて系外へ除かれる。この後、同条
件で2時間反応させて反応を完結させる。
Production Example 1 Ethylene oxide (hereinafter referred to as 12-hydrocystearic acid)
Equipped with a stirring rod, a thermometer, a dropping funnel and a Claisen tube equipped with 46,6 g of a compound obtained by block addition of 20 molar equivalents of EO) and 10 molar equivalents of propylene oxide (hereinafter, referred to as PO) and sodium monochloroacetate. 4 mouths 1
Charge the reaction flask, and stir well, with the reaction temperature 80 ~
While maintaining a reduced pressure of 50 mm / Hg at 85 ° C., 9.5 g of NaOH is added dropwise as a 48% aqueous solution over 1 hour. The water distilled at this time is condensed by the cooler and removed to the outside of the system. Thereafter, the reaction is carried out for 2 hours under the same conditions to complete the reaction.

製造例2 ジ−3−ヒドロキシラウリン酸ポリオキシエチレン
(以下POEと記す)ポリオキシプロピレン(以下POPと記
す)トリメチロールプロパンエステル(EO=60モル、
PO=50モル、ここでは平均付加モル数を意味する。
以下同じ)488.8gとモノクロロ酢酸ナトリウム8.3g及び
NaOH2.9gを40%水溶液として製造例と同様の操作を行な
って反応させた。
Production Example 2 Polyoxyethylene di-3-hydroxylaurate (hereinafter abbreviated as POE) polyoxypropylene (hereinafter abbreviated as POP) trimethylolpropane ester (EO = 60 mol,
PO = 50 moles, here means the average number of moles added.
The same applies hereinafter) 488.8 g, sodium monochloroacetate 8.3 g and
The reaction was carried out by performing the same operation as in the production example using 2.9 g of NaOH as a 40% aqueous solution.

製造例3 硬化ヒマシ油にEO=50モル、PO=30モルをランダム付
加させた化合物441.6gとモノブロムプロピオン酸ナトリ
ウム47.6g及びNaOH10.9gを40%水溶液として製造例1と
同様の操作を行なって反応させた。
Production Example 3 The same operation as in Production Example 1 was carried out using 441.6 g of a compound obtained by randomly adding EO = 50 mol and PO = 30 mol to hydrogenated castor oil, 47.6 g of sodium monobromopropionate and 10.9 g of NaOH as a 40% aqueous solution. And reacted.

実施例1 市中回収新聞古紙を2×5cmに細断後、その一定量を
卓上離解機に入れ、その中に水及び苛性ソーダ(対原
料)1.0%(重量基準、以下同じ)、珪酸ソーダ(対原
料)3.0%、30%過酸化水素水(対原料)3.0%、表−1
に示す各種の脱墨剤(対原料)0.4%を加え、パルプ濃
度5%、55℃、20分離解した後、50℃にて60分間熟成し
た。その後水を加えてパルプ濃度を1.0%に希釈し、CaC
l2(対原料)1.0%を添加し、30℃にて10分間フロテー
ション処理を施した。フロテーション後のパルプスラリ
ーを6%濃度まで濃縮後、水を加えて1%濃度に希釈
し、TAPPIシートマシンにてパルプシートを作製した。
得られたパルプシートを測色色差計(拡散反射型)にて
白色度を測定し、画像解析装置(×100倍)にて全残イ
ンキ数、未剥離インキ数を測定した。また、フロテータ
ー液面上の泡沫層の高さ(3分時点)も測定した。
Example 1 A used newspaper collected in the market was shredded to 2 × 5 cm, and a certain amount of the waste paper was put into a table disintegrator, in which water and caustic soda (based on raw material) were 1.0% (weight basis, the same applies hereinafter), sodium silicate ( 3.0%, 30% hydrogen peroxide water (based on raw material) 3.0%, Table-1
After adding 0.4% of various deinking agents (based on raw materials) shown in (1), the pulp concentration was 5%, the mixture was separated at 55 ° C for 20 minutes, and then ripened at 50 ° C for 60 minutes. Then, water was added to dilute the pulp concentration to 1.0%, and CaC
l 2 (based on raw material) was added, and flotation treatment was performed at 30 ° C. for 10 minutes. The pulp slurry after flotation was concentrated to a 6% concentration, and then diluted to 1% concentration by adding water, and a pulp sheet was prepared using a TAPPI sheet machine.
The whiteness of the obtained pulp sheet was measured with a colorimeter (diffuse reflection type), and the total number of remaining inks and the number of unstripped inks were measured with an image analyzer (× 100). Further, the height of the foam layer on the flotator liquid surface (at 3 minutes) was also measured.

結果を表−2に示す。 Table 2 shows the results.

実施例2 市中回収新聞古紙を2×5cmに細断後、その一定量を
卓上離解機に入れ、その中に水及び苛性ソーダ(対原
料)1.0%、珪酸ソーダ3号(対原料)0.5%、表−3に
示す各種の脱墨剤(対原料)0.4%を加え、パルプ濃度
5%、45℃、20分離解後、パルプ濃度を18%になる様に
脱水し、その中に苛性ソーダ(対原料)1.5%、硅酸ソ
ーダ(対原料)2.5%、30%過酸化水素水(対原料)3.0
%を加えて混合した後、55℃、90分間、パルプ濃度15%
で熟成処理を行なった。その後パルプ濃度4%になる様
に水を加え卓上離解機で5分間離解処理を施し、更に水
を加えてパルプ濃度を1.0%に希釈し、CaCl2(対原料)
1.0%を添加し、30℃にて10分間フロテーション処理を
行った。フロテーション後のパルプスラリーを6%濃度
まで濃縮後、水を加えて1%濃度に希釈し、TAPPIシー
トマシンにてパルプシートを作製した。得られたパルプ
シートを測色色差計(拡散反射型)にて白色度を測定
し、画像解析装置(×100倍)にて全残インキ数、未剥
離インキ数を測定した。また、フロテーター液面上の泡
沫層の高さ(3分時点)も測定した。
Example 2 The used newspaper collected in the market was shredded to 2 × 5 cm, and a certain amount was put into a table disintegrator, in which water and caustic soda (based on raw material) were 1.0%, and sodium silicate 3 (based on raw material) was 0.5%. And 0.4% of various deinking agents (based on raw materials) shown in Table 3 were added. The pulp concentration was 5%, and after 45 minutes at 45 ° C, the pulp was dehydrated so that the pulp concentration became 18%. 1.5% for raw material, 2.5% for sodium silicate (for raw material), 30% aqueous hydrogen peroxide (for raw material) 3.0
After adding and mixing, the pulp concentration is 15% at 55 ° C for 90 minutes.
For aging treatment. Then, water was added to a pulp concentration of 4%, and the mixture was subjected to a defibration treatment for 5 minutes using a desktop disintegrator. Further, water was added to dilute the pulp concentration to 1.0%, and CaCl 2 (based on raw material) was added.
1.0% was added, and a flotation treatment was performed at 30 ° C. for 10 minutes. The pulp slurry after flotation was concentrated to a 6% concentration, and then diluted to 1% concentration by adding water, and a pulp sheet was prepared using a TAPPI sheet machine. The whiteness of the obtained pulp sheet was measured with a colorimeter (diffuse reflection type), and the total number of remaining inks and the number of unstripped inks were measured with an image analyzer (× 100). Further, the height of the foam layer on the flotator liquid surface (at 3 minutes) was also measured.

その結果を表−4に示す。 Table 4 shows the results.

実施例3 市中回収雑誌を2×5cmに細断後、その一定量を卓上
離解機に入れ、その中に水及び苛性ソーダ(対原料)0.
5%、珪酸ソーダ(対原料)1.5%、30%過酸化水素(対
原料)1.0%、表−5に示す脱墨剤(対原料)0.05%を
加え、パルプ濃度15%、45℃で20分離解処理を行った。
その後この中へ水を加えてパルプ濃度4.0%に希釈し、
次いで更に水を加えてパルプ濃度を1.0%とした。これ
を30℃にて10分間フロテーション処理を施した。フロテ
ーション後のパルプスラリーを6%濃度まで濃縮後、水
を加えて1.0%濃度に希釈しTAPPIシートマシンにてパル
プシートを作製した。
Example 3 A city-collected magazine was cut into 2 × 5 cm pieces, and a certain amount was placed in a tabletop disintegrator, in which water and caustic soda (based on raw materials) were added.
5%, sodium silicate (based on raw material) 1.5%, 30% hydrogen peroxide (based on raw material) 1.0%, and a deinking agent (based on raw material) 0.05% shown in Table 5 are added. Separation solution processing was performed.
Then add water to this to dilute the pulp concentration to 4.0%,
Then, water was further added to bring the pulp concentration to 1.0%. This was subjected to a flotation treatment at 30 ° C. for 10 minutes. After the pulp slurry after the flotation was concentrated to a 6% concentration, water was added to dilute the pulp slurry to a 1.0% concentration to prepare a pulp sheet using a TAPPI sheet machine.

得られたパルプシートを測色色差計(拡散反射型)に
て白色度を測定し、画像解析装置(×100倍)にて全残
インキ数、未剥離インキ数を測定した。また、フロテー
ター液面上の泡沫層の高さ(3分経過時点)も測定し
た。
The whiteness of the obtained pulp sheet was measured with a colorimeter (diffuse reflection type), and the total number of remaining inks and the number of unstripped inks were measured with an image analyzer (× 100). In addition, the height of the foam layer on the flotator liquid surface (after 3 minutes) was also measured.

その結果を表−6に示す。 The results are shown in Table-6.

表−2、表−4及び表−6より、本発明の古紙再生用
脱墨剤によれば、白色度が高く、残インキ数も少なく、
特にその中でも未剥離インキ数が少ない良品質の脱墨パ
ルプを得ることができる。また、フロテーターでの操業
性の指標となる泡沫高も適切である。
From Table-2, Table-4 and Table-6, according to the used paper recycling deinking agent of the present invention, whiteness is high, the number of remaining inks is small,
In particular, high quality deinked pulp having a small number of unstripped inks can be obtained. In addition, the foam height, which is an index of the operability of the flotator, is also appropriate.

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】下記(A),(B)又は(C)で表される
OH基を含有する化合物とモノハロゲン低級カルボン酸塩
との反応生成物を有効成分とする古紙再生用脱墨剤。 (A); 炭素数5〜24のヒドロキシ脂肪酸にエチレンオキシドと
プロピレンオキシドとをエチレンオキシド/プロピレン
オキシド=1〜4(モル比)の割合となるように両者合
計で平均10〜50モル付加させた化合物 (B); エチレンオキシドとプロピレンオキシドとをエチレンオ
キシド/プロピレンオキシド=1〜4(モル比)の割合
となるように両者合計でOH基1個当たり平均10〜50モル
付加させたアルコールと、炭素数5〜24のヒドロキシ脂
肪酸とのエステル化合物 (C); 炭素数5〜24のヒドロキシ脂肪酸とアルコールとのエス
テルにエチレンオキシドとプロピレンオキシドとをエチ
レンオキシド/プロピレンオキシド=1〜4(モル比)
の割合となるように両者合計でOH基1個当たり平均10〜
50モル付加させた化合物
(1) Represented by the following (A), (B) or (C)
A deinking agent for recycling used paper, which comprises, as an active ingredient, a reaction product of a compound containing an OH group and a monohalogen lower carboxylate. (A); a compound obtained by adding an average of 10 to 50 mol of ethylene oxide and propylene oxide to a hydroxy fatty acid having 5 to 24 carbon atoms in a ratio of ethylene oxide / propylene oxide = 1 to 4 (molar ratio) in total. B) an alcohol obtained by adding an average of 10 to 50 moles of ethylene oxide and propylene oxide so as to have a ratio of ethylene oxide / propylene oxide of 1 to 4 (molar ratio) per OH group; Ester compound with hydroxy fatty acid of 24 (C); ester of hydroxy fatty acid having 5 to 24 carbon atoms and alcohol, ethylene oxide and propylene oxide being ethylene oxide / propylene oxide = 1 to 4 (molar ratio)
The average is 10 to 10 per OH group in total so that the ratio of
Compound with 50 moles added
【請求項2】化合物(A)、エステル(B)又は化合物
(C)の残存OH基1個当たり、0.8〜1.2モルのモノハロ
ゲン低級カルボン酸塩を使用する請求項1記載の古紙再
生用脱墨剤。
2. The method according to claim 1, wherein 0.8 to 1.2 mol of a monohalogen lower carboxylate is used per residual OH group of the compound (A), ester (B) or compound (C). Black ink.
【請求項3】アルコールが、炭素数1〜24の一価のアル
キルもしくはアルケニルアルコール又は多価アルコール
である請求項1又は2記載の古紙再生用脱墨剤。
3. The deinking agent according to claim 1, wherein the alcohol is a monovalent alkyl or alkenyl alcohol having 1 to 24 carbon atoms or a polyhydric alcohol.
JP33446390A 1990-11-30 1990-11-30 Deinking agent for recycled paper Expired - Fee Related JP2810538B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33446390A JP2810538B2 (en) 1990-11-30 1990-11-30 Deinking agent for recycled paper

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33446390A JP2810538B2 (en) 1990-11-30 1990-11-30 Deinking agent for recycled paper

Publications (2)

Publication Number Publication Date
JPH04202884A JPH04202884A (en) 1992-07-23
JP2810538B2 true JP2810538B2 (en) 1998-10-15

Family

ID=18277674

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33446390A Expired - Fee Related JP2810538B2 (en) 1990-11-30 1990-11-30 Deinking agent for recycled paper

Country Status (1)

Country Link
JP (1) JP2810538B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB9422878D0 (en) * 1994-11-12 1995-01-04 Stephenson Group Recycling of fibre products

Also Published As

Publication number Publication date
JPH04202884A (en) 1992-07-23

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