JP2761948B2 - Deinking agent for recycled paper - Google Patents

Deinking agent for recycled paper

Info

Publication number
JP2761948B2
JP2761948B2 JP29316489A JP29316489A JP2761948B2 JP 2761948 B2 JP2761948 B2 JP 2761948B2 JP 29316489 A JP29316489 A JP 29316489A JP 29316489 A JP29316489 A JP 29316489A JP 2761948 B2 JP2761948 B2 JP 2761948B2
Authority
JP
Japan
Prior art keywords
deinking agent
ink
pulp
deinking
dicarboxylic acid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
JP29316489A
Other languages
Japanese (ja)
Other versions
JPH03152284A (en
Inventor
進 門野
幸義 川守
芳春 橋口
良計 井上
正男 浜田
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 KASEI KK
Original Assignee
HARIMA KASEI KK
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 KASEI KK filed Critical HARIMA KASEI KK
Priority to JP29316489A priority Critical patent/JP2761948B2/en
Priority to US07/568,881 priority patent/US5158697A/en
Priority to DE19914110762 priority patent/DE4110762C2/en
Priority to FR9104061A priority patent/FR2674871B1/en
Priority to GB9108623A priority patent/GB2255111B/en
Publication of JPH03152284A publication Critical patent/JPH03152284A/en
Application granted granted Critical
Publication of JP2761948B2 publication Critical patent/JP2761948B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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、ちらし等の印刷古紙再生に用
いられる脱墨剤に関する。さらに詳しくは新聞、雑誌等
をフローテーション法で脱墨処理するに際し、発砲性、
インキ捕集性を高め、高白色度で残インキの少ない脱墨
パルプを得ることができる脱墨剤に関する。
Description: TECHNICAL FIELD The present invention relates to a deinking agent used for recycling printed waste paper such as newspapers, magazines, and leaflets. More specifically, when deinking newspapers and magazines by the flotation method,
The present invention relates to a deinking agent capable of improving ink collecting properties and obtaining a deinked pulp having high whiteness and little residual ink.

(従来の技術) 新聞、雑誌等の再生利用は古くから行われてきている
が、特に最近は森林資源の保護や脱墨パルプの用途拡大
により、古紙の有効利用はその重要性を増してきてい
る。
(Prior art) Recycling of newspapers, magazines, etc. has been practiced for a long time, but the importance of the effective use of waste paper has been increasing, especially in recent years, due to the protection of forest resources and the expanded use of deinked pulp. I have.

印刷古紙を再生するには、印刷古紙を通常離解機内で
苛性ソーダ、硅酸ソーダ等のアルカリ薬剤と脱墨剤、さ
らに必要に応じて過酸化水素、次亜硫酸塩等の漂白剤、
EDTA、DTPA等の金属イオン封鎖剤と共に離解し、パルプ
からインキを脱離させ、脱離したインキを水洗浄処理や
フローテーション処理によりパルプから分離する方法が
広く採用されている。
In order to recycle printed waste paper, the printed waste paper is usually treated in a disintegrator with an alkaline agent such as caustic soda and sodium silicate and a deinking agent, and, if necessary, a bleaching agent such as hydrogen peroxide and hyposulfite.
2. Description of the Related Art A method is widely used in which deflocculation is carried out together with a sequestering agent such as EDTA and DTPA, ink is detached from pulp, and the detached ink is separated from pulp by a water washing treatment or a flotation treatment.

脱墨剤には、大別して、離脱したインキを細かく分散
させた状態で系外に除去することを目的とする分散系脱
墨剤と、離脱したインキをある程度凝集させた状態で系
外に除去することを目的とする凝集系脱墨剤があり、こ
のうち現在では再生パルプの白色度をより高めることの
できる凝集系脱墨剤が広く用いられている。
The deinking agent is roughly divided into a dispersing deinking agent that aims to remove the detached ink finely dispersed outside the system, and a detached ink that is removed out of the system in a state where the detached ink is aggregated to some extent. There is an agglomerated deinking agent for the purpose of cleaning, and among them, an agglomerated deinking agent capable of further increasing the whiteness of recycled pulp is widely used.

脱墨剤としては、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、αオレフィンスルホン酸塩
等の陰イオン活性剤、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キルアリルエーテ
ル、脂肪酸アルカノールアマイド等の非イオン活性剤あ
るいは高級脂肪酸などが単独または2種以上配合されて
きた。しかしながら従来の脱墨剤で高級脂肪酸は、イン
キ凝集効果は高いが、パルプへの浸透、インキ剥離効果
が低く、充分な脱墨効果が得られない問題があり、ポリ
オキシアルキレンアルキルエーテルなどアルキレンオキ
シド付加物系(例えば特公昭64−11756号、特開昭63−3
03190号および特開平1−111086号)はパルプへの浸
透、インキ剥離分散効果が高いがインキとの親和性に劣
るため、インキの凝集効果が未だ充分でない。
Examples of deinking agents include anionic surfactants such as alkylbenzene sulfonates, higher alcohol sulfates, and α-olefin sulfonates, and nonionic surfactants such as polyoxyalkylene alkyl ethers, polyoxyalkylene alkyl allyl ethers, and fatty acid alkanolamides. Alternatively, higher fatty acids and the like have been used alone or in combination of two or more. However, higher fatty acids in conventional deinking agents have a high ink aggregating effect, but have a problem in that the penetration into the pulp and the ink releasing effect are low and a sufficient deinking effect cannot be obtained, and alkylene oxides such as polyoxyalkylene alkyl ethers are used. Adducts (for example, JP-B-64-11756, JP-A-63-3)
No. 03190 and Japanese Patent Application Laid-Open No. 1-111086) have a high effect of penetrating into pulp and dispersing and dispersing the ink, but have a poor affinity for the ink, so that the effect of coagulating the ink is not yet sufficient.

(本発明が解決しようとする問題点) 特に、最近の古紙は印刷技術の向上、特に印刷インキ
のオフセット化でインキ組成が変化し、乾性油や熱硬化
性樹脂が用いられており、このためインキ皮膜が強固に
硬化しており、従来の脱墨剤ではインキを脱離し、パル
プから分離することが難しく、高品質の脱墨パルプを得
ることができなかった。
(Problems to be Solved by the Present Invention) In particular, in recent waste paper, the ink composition has changed due to the improvement of printing technology, especially offset printing ink, and drying oil and thermosetting resin have been used. The ink film was hardened hard, and it was difficult to separate the ink with the conventional deinking agent and separate it from the pulp, so that high-quality deinked pulp could not be obtained.

また、脱墨パルプの用途拡大にともない、より高白色
度、残存インキの少ない脱墨パルプが求められている。
Further, with the expansion of uses of deinked pulp, deinked pulp having higher whiteness and less residual ink is required.

そこで、本発明はこれら離脱、分離の難しくなった古
紙についても容易に高脱墨の可能な脱墨剤を提供するこ
とを目的とする。
Accordingly, an object of the present invention is to provide a deinking agent capable of easily performing high deinking even on used paper that has become difficult to separate and separate.

(課題を解決するための手段) 本発明者らは上記目的を達成するためにはインキ剥離
効果が大きいと同時に、インキ凝集効果および適度の発
砲性の脱墨剤であることが必要であることに鑑み、鋭意
研究を重ねた結果、特定のジカルボン酸またはジカルボ
ン酸モノエステルにアルキレンオキシドを付加させたも
のは上記必要な物性を備えることを見出し、本発明を完
成した。
(Means for Solving the Problems) In order to achieve the above object, the present inventors need a deinking agent that has a large ink peeling effect, an ink aggregation effect, and an appropriate foaming property. In view of the above, as a result of intensive studies, they have found that a product obtained by adding an alkylene oxide to a specific dicarboxylic acid or dicarboxylic acid monoester has the above-mentioned necessary physical properties, and completed the present invention.

すなわち、本発明は下記の式(I) (ただし、Xの一方がCOO(AO)nHで、他方がHまたはC
H3でn=1〜200であり、AOはアルキレンオキシド、Y
は(AO)mHまたはRでm=1〜200、Rは炭素数1〜18
のアルキル基を示す) のジカルボン酸またはジカルボン酸モノエステルのアル
キレンオキシド付加物であることを要旨とする古紙再生
用脱墨剤にある。
That is, the present invention provides the following formula (I) (However, one of X is COO (AO) n H and the other is H or C
A n = 1 to 200 in H 3, AO is an alkylene oxide, Y
Is (AO) m H or R and m = 1 to 200, and R has 1 to 18 carbon atoms.
Which is an alkylene oxide adduct of a dicarboxylic acid or a dicarboxylic acid monoester of the formula (1).

本発明において使用される基本骨格のジカルボン酸は
式(II) (Xは式(1)の定義と同じ) で示され、特開昭49−66659号およびUSP第3899476号で
知られており、一般には商品名DIACID−1550(販売元:
播磨化成工業(株)ジカルボン酸90%、モノカルボン酸
9%、他不ケン化物の混合物)として販売されているも
のが利用でき、ジカルボン酸のモノエステルは、上記式
(II)で示されるジカルボン酸の1級カルボキシル機と
ROHで示されるアルコール(Rは炭素数1〜18、好まし
くは炭素数1〜15のアルキル基)、例えば、メタノー
ル、イソプロパノール、ブタノール、ヘキサノール、オ
クタノール、ラウリルアルコール、その他種々の合成ア
ルコールの単独または混合アルコールを公知の方法で反
応したものを利用することができる。本発明は少量のモ
ノマー酸の混入を制限するものではない。
The dicarboxylic acid of the basic skeleton used in the present invention has the formula (II) (X is the same as the definition of the formula (1)), which is known in JP-A-49-66659 and US Pat. No. 3,899,476, and generally has a trade name of DIACID-1550 (supplier:
Harima Chemicals, Inc. 90% of dicarboxylic acid, 9% of monocarboxylic acid, and a mixture of other unsaponifiable compounds can be used. The monoester of dicarboxylic acid is a dicarboxylic acid represented by the above formula (II). Primary acid carboxyl machine
Alcohol represented by ROH (R is an alkyl group having 1 to 18 carbon atoms, preferably 1 to 15 carbon atoms) such as methanol, isopropanol, butanol, hexanol, octanol, lauryl alcohol, and various other synthetic alcohols alone or in combination. A product obtained by reacting an alcohol by a known method can be used. The present invention does not limit the incorporation of small amounts of monomeric acids.

本発明において用いられるアルキレンオキシドとして
はエチレンオキシド、プロピレンオキシド、ブチレンオ
キシドが挙げられ、1種または2種以上を付加して良
く、2種以上の付加はランダム付加もしくはブロック付
加によって行うことができるが、エチレンオキシドとプ
ロピレンオキシドの組み合わせでランダムまたはブロッ
ク付加が最も好適である。アルキレンオキシドの付加モ
ル数は1〜200モルであり、200モル以上では脱墨でのフ
ローテーション工程の発砲性が低下し、また剥離したイ
ンキの凝集性を損ない、高品質の再生パルプが得られな
い。アルキレンオキシドの付加モル数は10〜120モルが
特に好適である。付加反応は特に限定されるものでな
く、例えば、上記ジカルボン酸またはジカルボン酸モノ
エステルにアルカリ性物質を触媒として加え、100〜200
℃、1〜5kg/cm2でアルキレンオキシドを吹き込み数時
間反応し、付加生成物を得ることができる。
Examples of the alkylene oxide used in the present invention include ethylene oxide, propylene oxide, and butylene oxide.One or more kinds may be added, and the addition of two or more kinds can be performed by random addition or block addition. Random or block addition is most preferred with a combination of ethylene oxide and propylene oxide. The addition mole number of the alkylene oxide is 1 to 200 moles, and if it is 200 moles or more, the foaming property of the flotation step in deinking is reduced, and the cohesiveness of the peeled ink is impaired, and high-quality recycled pulp is obtained. Absent. The addition mole number of the alkylene oxide is particularly preferably from 10 to 120 moles. The addition reaction is not particularly limited.For example, an alkaline substance is added as a catalyst to the dicarboxylic acid or dicarboxylic acid monoester, and 100 to 200
An alkylene oxide is blown at 1 ° C. and 1 to 5 kg / cm 2 and reacted for several hours to obtain an addition product.

本発明の脱墨剤の添加場所についてはパルパー、また
は熟成タワー前の工程が好ましいが、フローテーターに
添加使用することもできる。また本脱墨剤は単独で充分
効果的であるが、その他の脱墨剤、例えば陰イオン活性
剤やポリオキシアルキレンアルキルエーテルなどの非イ
オン活性剤、高級脂肪酸などを併用することも差し支え
ない。
The place where the deinking agent of the present invention is added is preferably a step before a pulper or an aging tower, but it can also be added to a floatator. Although the present deinking agent alone is sufficiently effective, other deinking agents, for example, nonionic activators such as anionic activators and polyoxyalkylene alkyl ethers and higher fatty acids may be used in combination.

(作用効果) 本発明の脱墨剤は特定のジカルボン酸またはジカルボ
ン酸モノエステルにアルキレンオキシドを付加している
ため、インキへの浸透、剥離性に優れるだけでなく、発
泡性およびまたインキの凝集性が従来の脱墨剤に比べ非
常に優れるため、高白色度で残インキの少ない高品質の
再生パルプを容易に得ることができる。
(Effects) Since the deinking agent of the present invention has an alkylene oxide added to a specific dicarboxylic acid or dicarboxylic acid monoester, it not only has excellent ink penetration and releasability, but also has good foaming properties and ink aggregation. Since the properties of the pulp are very superior to those of the conventional deinking agents, high-quality recycled pulp with high whiteness and little residual ink can be easily obtained.

(実施例) 以下、本発明を実施例に基づき具体的に説明する。(Examples) Hereinafter, the present invention will be specifically described based on examples.

〔実施例1〕 ジカルボン酸として平均分子量352.5のDIACID−1550
(販売元:播磨化成工業(株))352.5gを耐圧反応容器
に入れ、触媒として苛性カリ2.1gを加え、170℃に加熱
し、容器内を窒素ガスに置換し減圧脱気後、エチレンオ
キシド264.3gを圧力1〜5kg/cm2で3時間かけて吹き込
み反応し、エチレンオキシド6モル付加物の脱墨剤を得
た。
Example 1 DIACID-1550 having an average molecular weight of 352.5 as a dicarboxylic acid
(Distributor: Harima Kasei Kogyo Co., Ltd.) Put 352.5 g in a pressure-resistant reaction vessel, add 2.1 g of caustic potash as a catalyst, heat to 170 ° C., replace the inside of the vessel with nitrogen gas, degas under reduced pressure, and then 264.3 g of ethylene oxide Was blown at a pressure of 1 to 5 kg / cm 2 for 3 hours to obtain a deinking agent having 6 mol of ethylene oxide adduct.

〔実施例2〕 反応条件としてエチレンオキシドを881.0gとした以外
は実施例1と同様にしてエチレンオキシド20モル付加物
の脱墨剤を得た。
Example 2 A deinking agent was obtained in the same manner as in Example 1 except that the reaction conditions were changed to 881.0 g of ethylene oxide.

〔実施例3〕 DIACID−1550(販売元:播磨化成工業(株))と過剰
量のメチルアルコールを硫酸触媒を用いメタノール還流
状態下で反応してモノエステルとした後、過剰メチルア
ルコールを減圧除去した後、分子蒸留により精製して酸
価113、平均分子量367のモノエステルを得た。このモノ
エステル180.0gを耐圧反応容器に入れ、触媒として苛性
リ1.1gを加え、170℃に加熱し、容器内を窒素ガスに置
換し減圧脱気後、エチレンオキシド649.0gを1〜5kg/cm
2で3時間かけて吹き込み反応し、次いでプロピレンオ
キシド285.3gを圧力1〜5kg/cm2で5時間かけて吹き込
み反応してエチレンオキシド30モルおよびプロピレンオ
キシド10モル付加の脱墨剤を得た。
[Example 3] DIACID-1550 (sold by Harima Kasei Kogyo Co., Ltd.) and an excess amount of methyl alcohol were reacted under reflux of methanol using a sulfuric acid catalyst to form a monoester, and the excess methyl alcohol was removed under reduced pressure. After that, purification was performed by molecular distillation to obtain a monoester having an acid value of 113 and an average molecular weight of 367. 180.0 g of this monoester was placed in a pressure-resistant reaction vessel, 1.1 g of caustic was added as a catalyst, heated to 170 ° C., the inside of the vessel was replaced with nitrogen gas, and after degassing under reduced pressure, 649.0 g of ethylene oxide was added at 1 to 5 kg / cm.
Blowing reaction was carried out for 3 hours at 2 and then 285.3 g of propylene oxide was blown at a pressure of 1 to 5 kg / cm 2 for 5 hours to obtain a deinking agent with addition of 30 mol of ethylene oxide and 10 mol of propylene oxide.

〔実施例4〕 DIACID−1550とオクチルアルコールを200〜250℃で脱
水反応してモノエステルとした後、過剰のオクチルアル
コールを減圧除去し酸価89、平均分子量465のモノエス
テルを得た。このモノエステル180.0gを耐圧反応容器に
入れ、触媒として苛性カリ1.1gを加え、170℃に加熱
し、容器内を窒素ガスに置換し減圧脱気後、エチレンオ
キシド682.5gを圧力1〜5kg/cm2で3時間かけて吹き込
み反応、次いでプロピレンオキシド337.5gを圧力1〜5k
g/cm2で5時間かけて吹き込み反応してエチレンオキシ
ド40モルおよびプロビレンオキシド15モル付加の脱墨剤
を得た。
Example 4 DIACID-1550 and octyl alcohol were dehydrated at 200 to 250 ° C. to form a monoester, and then excess octyl alcohol was removed under reduced pressure to obtain a monoester having an acid value of 89 and an average molecular weight of 465. 180.0 g of this monoester was placed in a pressure-resistant reaction vessel, 1.1 g of caustic potassium was added as a catalyst, heated to 170 ° C., the inside of the vessel was replaced with nitrogen gas, and after degassing under reduced pressure, 682.5 g of ethylene oxide was pressured at 1 to 5 kg / cm 2. For 3 hours, and then 337.5 g of propylene oxide at a pressure of 1 to 5 k.
Blowing reaction was performed at g / cm 2 for 5 hours to obtain a deinking agent to which 40 mol of ethylene oxide and 15 mol of propylene oxide were added.

〔実施例5〕 DIACID−1550とラウリルアルコールを200〜250℃で反
応してモノエステルとした後、過剰のラウリルアルコー
ルを減圧除去し酸価78、平均分子量521のモノエステル
を得た。このモノエステル180.0gを耐圧反応容器に入
れ、触媒として苛性カリ1.1gを加え、170℃に加熱し、
容器内を窒素ガスに置換し減圧脱気後、エチレンオキシ
ド609.0gを圧力1〜5kg/cm2で3時間かけて吹き込み反
応、次いでプロピレンオキシド100.4kgを圧力1〜5kg/c
m2で5時間かけて吹き込み反応してエチレンオキシド40
モルおよびプロピレンオキシド5モル付加の脱墨剤を得
た。
Example 5 DIACID-1550 and lauryl alcohol were reacted at 200 to 250 ° C. to form a monoester, and excess lauryl alcohol was removed under reduced pressure to obtain a monoester having an acid value of 78 and an average molecular weight of 521. 180.0 g of this monoester was placed in a pressure-resistant reaction vessel, 1.1 g of caustic potassium was added as a catalyst, and the mixture was heated to 170 ° C.
After the inside of the vessel was replaced with nitrogen gas and degassed under reduced pressure, 609.0 g of ethylene oxide was blown in at a pressure of 1 to 5 kg / cm 2 for 3 hours, and then 100.4 kg of propylene oxide was pressured at 1 to 5 kg / c.
m 2 for 5 hours to give ethylene oxide 40
A deinking agent was obtained with the addition of 5 moles and 5 moles of propylene oxide.

〔実施例6〕 ジカルボン酸として平均分子量352.5のDAICID−1550
の115.0gを耐圧反応容器に入れ、触媒として苛性カリ0.
7gを加え、170℃に加熱し、容器内を窒素ガスに置換し
減圧脱気後、エチレンオキシド862.3gを圧力1〜5kg/cm
2で4時間かけて吹き込み反応、次いでプロピレンオキ
シド189.5gを圧力1〜5kg/cm2で4時間かけて吹き込み
反応してエチレンオキシド60モルおよびプロビレンオキ
シド10モル付加の脱墨剤を得た。
Example 6 DAICID-1550 having an average molecular weight of 352.5 as a dicarboxylic acid
Into a pressure-resistant reaction vessel, and 0.1% of caustic potassium was used as a catalyst.
7 g, heated to 170 ° C., the atmosphere in the container was replaced with nitrogen gas, and after degassing under reduced pressure, 862.3 g of ethylene oxide was pressured at 1 to 5 kg / cm.
Blowing reaction was carried out for 2 hours at 2 , followed by blowing reaction of 189.5 g of propylene oxide at a pressure of 1 to 5 kg / cm 2 for 4 hours to obtain a deinking agent with addition of 60 mol of ethylene oxide and 10 mol of propylene oxide.

〔実施例7〕 反応条件としてプロピレンオキシド吹き込み後、エチ
レンオキシドを吹き込み反応した以外は実施例6と同様
にして、プロピレンオキシド10モルおよびエチレンオキ
シド60モル付加の脱墨剤を得た。
Example 7 A deinking agent was prepared in the same manner as in Example 6, except that propylene oxide was blown in and ethylene oxide was blown in as a reaction condition, followed by addition of 10 moles of propylene oxide and 60 moles of ethylene oxide.

〔実施例8〕 反応条件としてエチレンオキシドとプロピレンオキシ
ドを同時に6時間かけて吹き込み反応した以外は実施例
6と同様にしてエチレンオキシド60モルおよびプロピレ
ンオキシド10モルのランダム付加の脱墨剤を得た。
Example 8 A deinking agent obtained by random addition of 60 mol of ethylene oxide and 10 mol of propylene oxide was obtained in the same manner as in Example 6, except that ethylene oxide and propylene oxide were simultaneously blown for 6 hours as reaction conditions.

〔実施例9〕 反応条件としてアルキレンオキシドをエチレンオキシ
ド574.8g、ブチレンオキシド141.1gとした以外は実施例
6と同様にして、エチレンオキシド40モルおよびブチレ
ンオキシド6モル付加の脱墨剤を得た。
Example 9 A deinking agent obtained by adding 40 mol of ethylene oxide and 6 mol of butylene oxide was obtained in the same manner as in Example 6, except that the alkylene oxide was changed to 574.8 g of ethylene oxide and 141.1 g of butylene oxide as reaction conditions.

〔実施例10〕 反応条件としてエチレンオキシド1724.5gを6時間
で、プロピレンオキシド757.9gを8時間で吹き込み反応
した以外は実施例6と同様にしてエチレンオキシド120
モルおよびプロピレンオキシド40モルの付加の脱墨剤を
得た。
Example 10 The same procedure as in Example 6 was repeated except that 1724.5 g of ethylene oxide was blown in for 6 hours and 757.9 g of propylene oxide were blown in for 8 hours.
An additional deinking agent of 40 moles and 40 moles of propylene oxide was obtained.

〔比較例2〜4〕 上記ジカルボン酸またはジカルボン酸モノエステルの
代わりにオレイン酸、ステアリン酸、およびラウリルア
ルコールを用い、実施例と同様の反応によりオレイン酸
(EO)20(PO)10、ステアリン酸(EO)20(PO)10、ラ
ウリルアルコール(EO)25(PO)10を得た。
[Comparative Examples 2 to 4] Using oleic acid, stearic acid, and lauryl alcohol in place of the above dicarboxylic acid or dicarboxylic acid monoester, oleic acid (EO) 20 (PO) 10 , stearic acid were obtained by the same reaction as in the example. (EO) 20 (PO) 10 and lauryl alcohol (EO) 25 (PO) 10 were obtained.

〔脱墨試験例〕[Example of deinking test]

J.TAPP紙パルプ試験法No.39−82に準じて、オフセッ
ト印刷新聞古紙80%とちらし20%からなる原料古紙を3
×3cmに細断し、一定量をパルプ離解機に入れ、温水を
入れ、古紙重量に対して苛性ソーダ1.5%、3号硅酸ソ
ーダ3.0%、30%過酸化水素水3.0%、表−1に示す各脱
墨剤0.3%を加え、パルプ濃度4.0%、50℃で30分離解し
た後、50℃で1時間熟成した。その後水を加えてパルプ
濃度1.0%に希釈し、30℃で10分間フローテーション処
理を行った。フローテーション後のパルプスラリーを80
メッシュワイヤーで脱水し5%に濃縮後、水を加えてパ
ルプ濃度1.0%に希釈し、角型シートマシンにて秤量100
g/m2のパルプシートを調製した。
In accordance with J.TAPP Pulp and Paper Test Method No.39-82, a raw material consisting of 80% offset printed newspaper waste paper and 20% leaflet waste paper was 3
Shred to × 3cm, put a certain amount into a pulp disintegrator, add warm water, 1.5% caustic soda, 3.0% sodium silicate 3.0%, 30% hydrogen peroxide 3.0% based on waste paper weight, Table 1 Each of the indicated deinking agents (0.3%) was added, the pulp concentration was 4.0%, the mixture was dissociated for 30 at 50 ° C, and then aged at 50 ° C for 1 hour. Thereafter, water was added to dilute the pulp to a concentration of 1.0%, followed by a flotation treatment at 30 ° C. for 10 minutes. 80 Pulp slurry after flotation
After dehydrating with a mesh wire and concentrating to 5%, water was added to dilute to a pulp concentration of 1.0%, and weighed 100 with a square sheet machine.
A pulp sheet of g / m 2 was prepared.

得られたパルプシートの白色度はJIS P8123に準じハ
ンター白色光度計で測定した。また残カーボン量の表示
は、脱墨パルプ中のカーボンの簡易測定法により、得ら
れたパルプシートを家庭用ミキサーで粉砕し、この100m
gをアセチルブロマイド/酢酸(1/3容量比)混合液に入
れ、65〜70℃、2時間でセルロースを溶解し、アドバン
テック東洋製グラスファイバーフィルター(GS25、直径
55mm)で濾過し、フィルターを風乾後、色差計にて測定
した。得れらた再生パルプシートの残存インキが少ない
ほど残カーボンL値は大きい値を示す。
The whiteness of the obtained pulp sheet was measured with a Hunter white light photometer according to JIS P8123. In addition, the indication of the residual carbon amount was obtained by crushing the obtained pulp sheet with a household mixer using a simple method of measuring carbon in deinked pulp.
g in an acetyl bromide / acetic acid (1/3 volume ratio) mixed solution, and dissolve cellulose at 65-70 ° C for 2 hours. Advantech Toyo glass fiber filter (GS25, diameter
After the filter was air-dried, it was measured with a color difference meter. The smaller the residual ink in the obtained recycled pulp sheet, the larger the residual carbon L value.

その結果を併せて表−1に示す。本発明の脱墨剤を使
用すると比較例1〜4の場合に比べ、白色度および残存
インキが減少することがわかる。
Table 1 also shows the results. It can be seen that when the deinking agent of the present invention is used, the whiteness and the residual ink are reduced as compared with Comparative Examples 1 to 4.

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】下記の式(I) (ただし、Xの一方がCOO(AO)nHで、他方がHまたはC
H3でn=1〜200であり、AOはアルキレンオキシド、Y
は(AO)mHまたはRでm=1〜200、Rは炭素数1〜18
のアルキル基を示す) のジカルボン酸またはジカルボン酸モノエステルのアル
キレンオキシド付加物を主成分とする古紙再生用脱墨
剤。
(1) The following formula (I) (However, one of X is COO (AO) n H and the other is H or C
A n = 1 to 200 in H 3, AO is an alkylene oxide, Y
Is (AO) m H or R and m = 1 to 200, and R has 1 to 18 carbon atoms.
And an alkylene oxide adduct of dicarboxylic acid or dicarboxylic acid monoester as a main component.
JP29316489A 1989-10-26 1989-11-09 Deinking agent for recycled paper Expired - Fee Related JP2761948B2 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP29316489A JP2761948B2 (en) 1989-11-09 1989-11-09 Deinking agent for recycled paper
US07/568,881 US5158697A (en) 1989-10-26 1990-08-17 Deinking agent for reproduction of printed waste papers
DE19914110762 DE4110762C2 (en) 1989-10-26 1991-04-03 Decolorizing agent for the processing of printed waste paper
FR9104061A FR2674871B1 (en) 1989-10-26 1991-04-03 DEINKING AGENT FOR THE REGENERATION OF OLD PRINTED PAPERS.
GB9108623A GB2255111B (en) 1989-10-26 1991-04-23 Deinking agent

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29316489A JP2761948B2 (en) 1989-11-09 1989-11-09 Deinking agent for recycled paper

Publications (2)

Publication Number Publication Date
JPH03152284A JPH03152284A (en) 1991-06-28
JP2761948B2 true JP2761948B2 (en) 1998-06-04

Family

ID=17791247

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29316489A Expired - Fee Related JP2761948B2 (en) 1989-10-26 1989-11-09 Deinking agent for recycled paper

Country Status (1)

Country Link
JP (1) JP2761948B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5880077A (en) * 1997-08-29 1999-03-09 High Point Chemical Corporation Wastepaper reclaiming deinking agent

Also Published As

Publication number Publication date
JPH03152284A (en) 1991-06-28

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