JP5593791B2 - Foreign matter removing agent for floatator in deinking step, foreign matter removing method, and method for producing deinked pulp - Google Patents

Foreign matter removing agent for floatator in deinking step, foreign matter removing method, and method for producing deinked pulp Download PDF

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JP5593791B2
JP5593791B2 JP2010084267A JP2010084267A JP5593791B2 JP 5593791 B2 JP5593791 B2 JP 5593791B2 JP 2010084267 A JP2010084267 A JP 2010084267A JP 2010084267 A JP2010084267 A JP 2010084267A JP 5593791 B2 JP5593791 B2 JP 5593791B2
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foreign matter
matter removing
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quaternary ammonium
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優子 大草
知成 加藤
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Kurita Water Industries Ltd
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    • 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
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    • Y02W30/64Paper recycling

Description

本発明は、脱墨工程におけるフローテーター用異物除去剤、異物除去方法、及び脱墨パルプの製造方法に関する。更に詳しくは、本発明は、古紙再生処理等の工程において、インク、灰分、ピッチ等を効率的に除去することができる脱墨工程におけるフローテーター用異物除去剤、異物除去方法、及び異物量が少なく、パルプの白色度に優れた脱墨パルプの製造方法に関する。   The present invention relates to a foreign matter removing agent for a floater, a foreign matter removing method, and a deinked pulp manufacturing method in a deinking step. More specifically, the present invention relates to a foreign matter removing agent for a floatator, a foreign matter removing method, and a foreign matter amount in a deinking process capable of efficiently removing ink, ash, pitch, and the like in a process such as used paper recycling processing. The present invention relates to a method for producing a deinked pulp having a low pulp whiteness.

近年、省エネルギー、省資源の立場から、印刷古紙の再利用が大きな課題となっている。印刷古紙を回収して再利用するために、脱墨工程によって印刷インク等を除去してパルプ繊維を採取し、脱墨パルプ(DIP)が製造されている。
一般に、脱墨パルプの製造方法は、主として離解工程、熟成工程、フローテーション工程、及び脱水・洗浄工程を含んでいる。離解工程は、剥離機を用いて機械的にインクを剥がす工程であり、熟成工程は、化学的にインクを剥がす工程である。これらの剥離及び熟成工程において、一般的に、アルカリ剤、漂白剤等の薬剤と共に、脱墨剤が用いられる。次に、フローテーション工程において、パルプとインクの混合物に気泡を吹き込み、泡にインク等の異物を付着させて浮上分離し、系外にフロス(脱墨パルプを取り出した後の残渣)として排出する。その後、得られたパルプスラリーは脱水・洗浄処理して適度な濃度に調整される。
In recent years, the reuse of used printed paper has become a major issue from the standpoint of energy saving and resource saving. In order to collect and reuse the used printing paper, printing ink is removed by a deinking process, and pulp fibers are collected to produce deinked pulp (DIP).
Generally, the method for producing deinked pulp mainly includes a disaggregation process, an aging process, a flotation process, and a dehydration / washing process. The disaggregation step is a step of mechanically removing ink using a peeling machine, and the aging step is a step of chemically removing ink. In these peeling and aging processes, a deinking agent is generally used together with a chemical such as an alkali agent and a bleaching agent. Next, in the flotation process, bubbles are blown into the mixture of pulp and ink, and foreign matters such as ink are attached to the bubbles and floated and separated, and discharged out of the system as floss (residue after taking out the deinked pulp). . Thereafter, the obtained pulp slurry is dehydrated and washed to be adjusted to an appropriate concentration.

このフローテーション工程は脱墨工程の中でも製品の品質を左右する重要な工程である。フローテーター(浮選機)によれば、一般に粒径5〜20μmの粒子が除去可能であるが、粒径5μm未満の粒子に対する除去性能は低いという問題がある。
フローテーション工程で用いられる脱墨剤としては、アルミニウム化合物等の無機凝集剤、高級アルコール又は脂肪酸のアルキレンオキサイド付加物系の界面活性剤、高級脂肪酸系薬剤の他、架橋したポリジアリルジメチルアンモニウムクロライドを含有する脱墨剤(特許文献1)、水溶性両性アクリルアミド系重合体を含有する異物除去剤(特許文献2)等が知られており、カチオン性化合物、アミン等の存在下に行う脱墨方法(例えば特許文献3)も知られている。
しかしながら、従来の脱墨剤や脱墨方法は、インクの剥離性と除去性についてある程度改善されているものの、インクの凝集性、灰分除去性は十分でない。
このために、古紙再生における、フローテーター用のインク除去性、灰分除去性の優れた異物除去剤、異物除去方法が求められていた。
This flotation process is an important process that affects the quality of the product among the deinking processes. According to a flotator (flotation machine), particles having a particle diameter of 5 to 20 μm can generally be removed, but there is a problem that the removal performance for particles having a particle diameter of less than 5 μm is low.
Deinking agents used in the flotation process include inorganic flocculants such as aluminum compounds, higher alcohol or fatty acid alkylene oxide adduct surfactants, higher fatty acid agents, and crosslinked polydiallyldimethylammonium chloride. Known deinking agents (Patent Literature 1), foreign matter removing agents containing water-soluble amphoteric acrylamide polymers (Patent Literature 2), etc. are known, and are deinking methods carried out in the presence of cationic compounds, amines, etc. (For example, patent document 3) is also known.
However, although conventional deinking agents and deinking methods have improved ink peeling and removal to some extent, ink aggregation and ash removal are not sufficient.
For this reason, there has been a demand for a foreign matter removing agent and a foreign matter removing method excellent in ink removability and ash content removal for a floater in used paper recycling.

特開2001−271284号公報JP 2001-271284 A 特開2002−115191号公報JP 2002-115191 A 特開平10−158985号公報JP-A-10-158985

本発明は、フローテーターでインク、灰分、ピッチ等の異物除去を効率的に行うことができる脱墨工程におけるフローテーター用異物除去剤、異物除去方法、及び脱墨パルプの製造方法を提供することを課題とする。   The present invention provides a foreign matter removing agent for a flowator, a foreign matter removing method, and a deinked pulp manufacturing method in a deinking step capable of efficiently removing foreign matter such as ink, ash, and pitch with a flowator. Is an issue.

本発明者は、前記目的を達成するために鋭意研究を重ねた結果、特定の第四級アンモニウム基含有モノマー由来の構成単位を有するカチオン性単独重合体又は共重合体を用いることにより、フローテーターでの異物除去を効率的に行うことができることを見出した。本発明は、かかる知見に基づいて完成したものである。
すなわち、本発明は、下記(1)〜(5)を提供するものである。
(1)下記一般式(1)で表される第四級アンモニウム基含有モノマー由来の構成単位を有するカチオン性単独重合体又は共重合体を含有することを特徴とする脱墨工程におけるフローテーター用異物除去剤。
As a result of intensive studies to achieve the above-mentioned object, the present inventor has used a cationic homopolymer or copolymer having a structural unit derived from a specific quaternary ammonium group-containing monomer to produce a flotator. It has been found that foreign matter removal can be performed efficiently. The present invention has been completed based on such findings.
That is, the present invention provides the following (1) to (5).
(1) For a floatator in a deinking step, comprising a cationic homopolymer or copolymer having a structural unit derived from a quaternary ammonium group-containing monomer represented by the following general formula (1) Foreign matter remover.

Figure 0005593791
Figure 0005593791

(式中、R1及びR2は水素原子又はメチル基を示し、R3及びR4は水素、炭素数1〜4のアルキル基、ピペラジン基、ピペリジン基又はモルホリン基を示し、R5は炭素数1〜22の炭化水素基を示し、Aは炭素数1〜5のアルカンジイル基を示し、Xは第四級アンモニウム基の対イオンを示す。)
(2)カチオン性単独重合体又は共重合体が、アクリルアミドモノマー由来の構成単位を0〜30モル%を含有するものである、前記(1)のフローテーター用異物除去剤。
(3)カチオン性単独重合体又は共重合体の重量平均分子量が10万〜200万である、前記(1)のフローテーター用異物除去剤。
(4)前記(1)の異物除去剤を、古紙の脱墨処理におけるフローテーション工程又はその前工程に添加することを特徴とする異物除去方法。
(5)脱墨工程のパルプスラリー中に、前記一般式(1)で表される第四級アンモニウム基含有モノマー由来の構成単位を有するカチオン性単独重合体又は共重合体を添加することを特徴とする脱墨パルプの製造方法。
(Wherein R 1 and R 2 represent a hydrogen atom or a methyl group, R 3 and R 4 represent hydrogen, an alkyl group having 1 to 4 carbon atoms, a piperazine group, a piperidine group or a morpholine group, and R 5 represents a carbon atom. (A represents a C 1-5 alkanediyl group, and X represents a counter ion of a quaternary ammonium group.)
(2) The foreign matter removing agent for a floatator according to (1), wherein the cationic homopolymer or copolymer contains 0 to 30 mol% of a structural unit derived from an acrylamide monomer.
(3) The foreign matter removing agent for a floatator according to (1), wherein the cationic homopolymer or copolymer has a weight average molecular weight of 100,000 to 2,000,000.
(4) A foreign matter removing method, wherein the foreign matter removing agent (1) is added to a flotation step or a preceding step in deinking treatment of waste paper.
(5) A cationic homopolymer or copolymer having a structural unit derived from a quaternary ammonium group-containing monomer represented by the general formula (1) is added to the pulp slurry in the deinking step. A method for producing deinked pulp.

本発明の異物除去剤、異物除去方法、及び脱墨パルプの製造方法によれば、フローテーターでインク、灰分、ピッチ等の異物除去を効率的に行うことができるため、脱墨パルプの白色度を向上させることができると共に、抄紙工程への異物持込量を低減することができる。
また、本発明の異物除去剤はパルプ繊維や灰分への定着性が低いため、パルプ繊維の歩留り(回収効率)に悪影響を与えることがない。更に、異物低減により排水負荷の低減が可能となり、古紙由来の灰分が除去できるため、抄紙工程における填料の種類、粒径の調整が容易となり、紙品質の向上を図ることができる。
According to the foreign matter removing agent, the foreign matter removing method, and the deinked pulp manufacturing method of the present invention, since the foreign matter such as ink, ash, and pitch can be efficiently removed with a floatator, the whiteness of the deinked pulp Can be improved, and the amount of foreign matter brought into the papermaking process can be reduced.
Moreover, since the foreign matter removing agent of the present invention has low fixability to pulp fibers and ash, it does not adversely affect the yield (recovery efficiency) of pulp fibers. Furthermore, since the waste water load can be reduced by reducing foreign matters and the ash content from waste paper can be removed, the type and particle size of the filler in the paper making process can be easily adjusted, and the paper quality can be improved.

[排水のフローテーター用異物除去剤]
(一般式(1)で表される第四級アンモニウム基含有モノマー)
本発明において、フローテーター用異物除去剤に用いられるカチオン性単独重合体又は共重合体は、下記一般式(1)で表される第四級アンモニウム基含有モノマー由来の構成単位を有する。この第四級アンモニウム基含有モノマーは重合体又は共重合体にカチオン性を付与するものである。
[Foreign substance remover for waste water floatator]
(Quaternary ammonium group-containing monomer represented by general formula (1))
In the present invention, the cationic homopolymer or copolymer used in the foreign matter removing agent for a floatator has a structural unit derived from a quaternary ammonium group-containing monomer represented by the following general formula (1). This quaternary ammonium group-containing monomer imparts cationicity to the polymer or copolymer.

Figure 0005593791
Figure 0005593791

一般式(1)において、R1及びR2は水素原子又はメチル基を示し、R3及びR4は水素、炭素数1〜4のアルキル基、ピペラジン基、ピペリジン基又はモルホリン基を示す。
5は炭素数1〜22の炭化水素基を示し、好ましくは炭素数1〜12、より好ましくは炭素数1〜8の炭化水素基を示し、より具体的には、炭素数1〜5のアルキル基、ベンジル基等が挙げられる。
Aは炭素数1〜5、好ましくは炭素数1〜4のアルカンジイル基を示す。Aの具体例としては、メチレン基、エチレン基、トリメチレン基、プロパン−1,2−ジイル基、テトラメチレン基等が挙げられる。
Xは第四級アンモニウム基の対イオンを示し、具体例としては、塩素イオン、ヨウ素イオン等のハロゲンイオン、硫酸イオン、亜硫酸イオン、過塩素酸イオン、リン酸イオン、ホウ酸イオン、又はp−トルエンスルホン酸イオン等の有機酸塩のアニオン等が挙げられる。
In the general formula (1), R 1 and R 2 represent a hydrogen atom or a methyl group, and R 3 and R 4 represent hydrogen, an alkyl group having 1 to 4 carbon atoms, a piperazine group, a piperidine group, or a morpholine group.
R 5 represents a hydrocarbon group having 1 to 22 carbon atoms, preferably a hydrocarbon group having 1 to 12 carbon atoms, more preferably a hydrocarbon group having 1 to 8 carbon atoms, and more specifically, a hydrocarbon group having 1 to 5 carbon atoms. Examples thereof include an alkyl group and a benzyl group.
A represents an alkanediyl group having 1 to 5 carbon atoms, preferably 1 to 4 carbon atoms. Specific examples of A include a methylene group, an ethylene group, a trimethylene group, a propane-1,2-diyl group, and a tetramethylene group.
X represents a counter ion of a quaternary ammonium group, and specific examples include halogen ions such as chlorine ions and iodine ions, sulfate ions, sulfite ions, perchlorate ions, phosphate ions, borate ions, or p- Examples include anions of organic acid salts such as toluenesulfonate ions.

一般式(1)で表される第四級アンモニウム基含有モノマーは、対応する第三級アミンと塩化メチル、塩化ベンジル、硫酸メチル等の四級化剤とを公知の方法により反応させることにより得ることができる。その具体例としては、ジアルキルアミノアルカンジイル(メタ)アクリルアミドの塩化メチル四級化物や塩化ベンジル四級化物等が挙げられる。
それらの中では、異物除去性能の観点から、下記一般式(2)で表される第四級アンモニウム基含有モノマーが好ましい。
The quaternary ammonium group-containing monomer represented by the general formula (1) is obtained by reacting a corresponding tertiary amine with a quaternizing agent such as methyl chloride, benzyl chloride, or methyl sulfate by a known method. be able to. Specific examples thereof include a methyl chloride quaternized product of dialkylaminoalkanediyl (meth) acrylamide and a benzyl chloride quaternized product.
Among them, a quaternary ammonium group-containing monomer represented by the following general formula (2) is preferable from the viewpoint of foreign matter removal performance.

Figure 0005593791
Figure 0005593791

一般式(2)において、R2は水素原子又はメチル基を示し、R3及びR4はメチル基又はエチル基を示し、R5は炭素数1〜3のアルキル基を示し、nは2又は3である。
その具体例としては、ジメチルアミノプロピルアクリルアミド(DMAPAA)の塩化メチル四級化物(アクリルアミドプロピルトリメチルアンモニウムクロリド)、ジメチルアミノエチルアクリルアミドの塩化メチル四級化物、ジメチルアミノプロピルメタクリルアミドの塩化メチル四級化物、ジメチルアミノエチルメタクリルアミドの塩化メチル四級化物等が挙げられる。
In the general formula (2), R 2 represents a hydrogen atom or a methyl group, R 3 and R 4 represent a methyl group or an ethyl group, R 5 represents an alkyl group having 1 to 3 carbon atoms, and n represents 2 or 3.
Specific examples thereof include dimethylaminopropylacrylamide (DMAPAA) methyl chloride quaternized product (acrylamidopropyltrimethylammonium chloride), dimethylaminoethylacrylamide methyl chloride quaternized product, dimethylaminopropyl methacrylamide methyl chloride quaternized product, Examples include methyl chloride quaternized product of dimethylaminoethyl methacrylamide.

(カチオン性共重合体)
本発明において、カチオン性共重合体を用いる場合、一般式(1)で表される第四級アンモニウム基含有モノマーとの共重合モノマーとしては、置換又は無置換のアクリルアミド及び/又はメタクリルアミドが好ましく挙げられる。その置換基としては、アミドの窒素原子に置換する、好ましくは炭素数1〜8、より好ましくは炭素数1〜5の直鎖又は分岐鎖のアルキル基が好ましい。
前記共重合モノマーの具体例としては、アクリルアミド、N−メチルアクリルアミド、N−エチルアクリルアミド、N−シクロプロピルアクリルアミド、N−イソプロピルアクリルアミド、メタクリルアミド、N−メチルメタクリルアミド、N−シクロプロピルメタクリルアミド、N−イソプロピルメタクリルアミド、N,N−ジメチルアクリルアミド、N−メチル−N−エチルアクリルアミド、N−メチル−N−イソプロピルアクリルアミド、N−メチル−N−n−プロピルアクリルアミド、N,N−ジエチルアクリルアミド等が挙げられる。これらの中では、機能性の観点から、アクリルアミド、N−メチルアクリルアミド、N−エチルアクリルアミド、N,N−ジメチルアクリルアミド等がより好ましい。
カチオン性共重合体は、前記共重合モノマー由来の構成単位を、好ましくは30モル%以下、より好ましくは20モル%以下、より好ましくは10モル%以下、更に好ましくは5モル%以下含有する。
(Cationic copolymer)
In the present invention, when a cationic copolymer is used, the copolymerized monomer with the quaternary ammonium group-containing monomer represented by the general formula (1) is preferably a substituted or unsubstituted acrylamide and / or methacrylamide. Can be mentioned. The substituent is preferably a linear or branched alkyl group having 1 to 8 carbon atoms, more preferably 1 to 5 carbon atoms, which is substituted on the nitrogen atom of the amide.
Specific examples of the copolymerization monomer include acrylamide, N-methylacrylamide, N-ethylacrylamide, N-cyclopropylacrylamide, N-isopropylacrylamide, methacrylamide, N-methylmethacrylamide, N-cyclopropylmethacrylamide, N -Isopropylmethacrylamide, N, N-dimethylacrylamide, N-methyl-N-ethylacrylamide, N-methyl-N-isopropylacrylamide, N-methyl-Nn-propylacrylamide, N, N-diethylacrylamide, etc. It is done. Among these, acrylamide, N-methylacrylamide, N-ethylacrylamide, N, N-dimethylacrylamide and the like are more preferable from the viewpoint of functionality.
The cationic copolymer preferably contains 30 mol% or less, more preferably 20 mol% or less, more preferably 10 mol% or less, and still more preferably 5 mol% or less of the structural unit derived from the copolymer monomer.

(カチオン性単独重合体又は共重合体の製造)
一般式(1)で表される第四級アンモニウム基含有モノマー由来の構成単位を有するカチオン性単独重合体又は共重合体の製造は、一般式(1)で表される第四級アンモニウム基含有モノマーを、所望により前記共重合モノマーと共に、水混和性溶媒、例えばイソプロパノール等のアルコールを含む水等の水性媒体中で、既知の重合法を用いて行うことができる。
重合に際しては、前記モノマーを重合開始剤を含む水性媒体中に滴下して行うことが好ましい。
重合開始剤として、少量のラジカル形成物質、例えばペルオクソ二硫酸カリウム又はアンモニウム、t−ブチルヒドロペルオキシド、アゾビス(イソブチロニトリル)等を用いることができる。
重合温度は特に限定されないが、用いる重合開始剤に応じて、5〜100℃が好ましく、10〜90℃がより好ましい。このようにして、ポリマー含量(固形分濃度)が好ましくは5〜60重量%、より好ましくは10〜50重量%の重合体又は共重合体のポリマー溶液を得ることができる。
前記重合体又は共重合体の重量平均分子量は、異物除去効果とパルプ歩留りの観点から、10万〜200万が好ましく、15万〜100万がより好ましい。なお、重量平均分子量は、例えば光散乱光度計等を用いた公知の方法により測定することができる。
(Production of cationic homopolymer or copolymer)
The production of a cationic homopolymer or copolymer having a structural unit derived from a quaternary ammonium group-containing monomer represented by the general formula (1) includes a quaternary ammonium group represented by the general formula (1). The monomers can be carried out using known polymerization methods in an aqueous medium such as water containing a water-miscible solvent, for example, an alcohol such as isopropanol, optionally together with the copolymerization monomer.
The polymerization is preferably performed by dropping the monomer into an aqueous medium containing a polymerization initiator.
As the polymerization initiator, a small amount of a radical forming substance such as potassium or ammonium peroxodisulfate, t-butyl hydroperoxide, azobis (isobutyronitrile) and the like can be used.
Although polymerization temperature is not specifically limited, 5-100 degreeC is preferable according to the polymerization initiator to be used, and 10-90 degreeC is more preferable. In this way, a polymer solution of a polymer or copolymer having a polymer content (solid content concentration) of preferably 5 to 60% by weight, more preferably 10 to 50% by weight can be obtained.
The weight average molecular weight of the polymer or copolymer is preferably 100,000 to 2,000,000, and more preferably 150,000 to 1,000,000 from the viewpoints of foreign matter removal effect and pulp yield. The weight average molecular weight can be measured by a known method using, for example, a light scattering photometer.

[異物除去方法]
本発明の異物除去方法は、前記一般式(1)で表される第四級アンモニウム基含有モノマー由来の構成単位を有するカチオン性単独重合体又は共重合体を含有する異物除去剤を、古紙の脱墨処理におけるフローテーション工程又はその前工程に添加することを特徴とし、これにより、パルプ繊維と、インク、灰分、ピッチ等の異物とを効率的に分離、除去することができる。
[Foreign matter removal method]
In the foreign matter removing method of the present invention, a foreign matter removing agent containing a cationic homopolymer or copolymer having a structural unit derived from a quaternary ammonium group-containing monomer represented by the general formula (1) is used. It is characterized by being added to the flotation step in the deinking process or a previous step thereof, whereby pulp fibers and foreign matters such as ink, ash, and pitch can be efficiently separated and removed.

(脱墨処理におけるフローテーション工程への適用)
古紙の脱墨処理においては、前記カチオン性単独重合体又は共重合体を含有する異物除去剤を、フローテーション工程又はその前工程に添加して、フローテーション処理を行う。
脱墨パルプ製造工程の原料は、一般に強いアニオン性を示すSS(懸濁物質)が分散した状態にある。このような強いアニオン性を有するSSに対して、本発明の異物除去剤は、前記一般式(1)で表される第四級アンモニウム基含有モノマー由来の構成単位を有するカチオン性単独重合体又は共重合体を含有するため、その荷電中和作用、凝結作用により、コロイド状SSの粒子径をフローテーターで処理可能な大きさに成長させることができるため、本発明の優れた効果を得ることができると考えられる。また、本発明の異物除去剤は、パルプ繊維や灰分への定着性が低いため、パルプ繊維の歩留りに影響を与えず、異物成分のみを効率的に排出できる。
(Application to flotation process in deinking process)
In the deinking treatment of used paper, the foreign matter removing agent containing the cationic homopolymer or copolymer is added to the flotation step or the previous step to perform the flotation treatment.
The raw material for the deinked pulp manufacturing process is generally in a state where SS (suspended substance) showing strong anionicity is dispersed. For the SS having such strong anionicity, the foreign substance removing agent of the present invention is a cationic homopolymer having a structural unit derived from a quaternary ammonium group-containing monomer represented by the general formula (1) or Since the copolymer is contained, the particle size of the colloidal SS can be grown to a size that can be processed by a flowmeter by the charge neutralization action and the coagulation action, thereby obtaining the excellent effect of the present invention. It is thought that you can. Further, since the foreign matter removing agent of the present invention has low fixability to pulp fibers and ash, it can efficiently discharge only foreign matter components without affecting the yield of pulp fibers.

異物除去剤の添加方法に特に制限はないが、水溶液として添加することが好ましい。
異物除去剤はフローテーターのみならず、その任意の前工程、例えば、パルパー、ニーダー、タワー、パルパーとニーダーの間にある脱水機、又はこれらをつなぐ配管等に添加することができる。
ここで、本発明におけるフローテーターとしては、脱墨を主目的とする一次フローテーターのみならず、一次フローテーターから排出されるフロスを処理する二次フローテーターや、フローテーター後の洗浄工程から排出される排水を処理する回収再利用水系等に設置したフローテーターも含まれる。
Although there is no restriction | limiting in particular in the addition method of a foreign material removal agent, Adding as aqueous solution is preferable.
The foreign matter removing agent can be added not only to the floatator but also to any preceding step, for example, a pulper, a kneader, a tower, a dehydrator between the pulper and the kneader, or a pipe connecting them.
Here, as the flowator in the present invention, not only the primary flowator mainly used for deinking, but also the secondary flowator for treating the floss discharged from the primary flowator and the cleaning process after the flowator are discharged. It also includes a floatator installed in a recovery / reuse water system that treats wastewater.

異物除去剤の添加量に特に制限はないが、フローテーター処理に当たり、前記カチオン性単独重合体又は共重合体を、処理原水に対し、好ましくは0.5〜100mg/L、より好ましくは1〜80mg/L、更に好ましくは5〜60mg/L添加することが望ましい。添加量が前記範囲内であると、異物除去効果は十分であり、パルプ繊維のフロスヘの移行が進み過ぎてパルプの歩留りが低下するという不都合もない。
異物除去剤の添加の際には、得られる脱墨パルプの白色度及び灰分含有量を測定することによって、異物除去剤の添加量を調節することができる。
本発明の異物除去方法は、すでに剥離されたインク、灰分、ピッチ等を凝集させてパルプ繊維から分離する効果に優れているが、更にインク剥離機能に優れた公知の有機脱墨剤(界面活性剤)、起泡剤等の助剤を合わせて添加することができる。
Although there is no restriction | limiting in particular in the addition amount of a foreign material removal agent, Preferably it is 0.5-100 mg / L with respect to the process raw | natural water in the said cationic homopolymer or copolymer in a floater process, More preferably, 1- It is desirable to add 80 mg / L, more preferably 5 to 60 mg / L. When the added amount is within the above range, the foreign matter removing effect is sufficient, and there is no inconvenience that the pulp fiber is excessively transferred to the floss and the pulp yield is lowered.
When the foreign matter removing agent is added, the added amount of the foreign matter removing agent can be adjusted by measuring the whiteness and ash content of the resulting deinked pulp.
The foreign matter removing method of the present invention is excellent in the effect of aggregating already peeled ink, ash, pitch, etc. and separating from the pulp fiber, but further known organic deinking agents (surfactant) Agent) and auxiliary agents such as foaming agents can be added together.

[脱墨パルプの製造方法]
本発明の脱墨パルプの製造方法は、脱墨工程のパルプスラリー中に、下記一般式(1)で表される第四級アンモニウム基含有モノマー由来の構成単位を有するカチオン性単独重合体又は共重合体を添加することを特徴とする。
[Method for producing deinked pulp]
The deinked pulp production method of the present invention comprises a cationic homopolymer or copolymer having a structural unit derived from a quaternary ammonium group-containing monomer represented by the following general formula (1) in the pulp slurry of the deinking step. It is characterized by adding a polymer.

Figure 0005593791
(式中、R1、R2、R3、R4、R5、A、及びXは前記と同様である。)
Figure 0005593791
(In the formula, R 1 , R 2 , R 3 , R 4 , R 5 , A, and X are the same as described above.)

(脱墨パルプの具体的な製造例)
本発明における脱墨パルプの製造は、従来公知の脱墨パルプの製造方法と同様にして行うことができる。例えば、まず水酸化ナトリウム、ケイ酸ナトリウム等のアルカリを含む水に原料古紙を加え、パルパー(パルプ離解装置)で古紙を離解してパルプスラリー化した後、ニーダーでパルプスラリーと脱墨剤(例えばノニオン性界面活性剤)を混練し、印刷インクをパルプから引き剥がす。次いで、過酸化水素を加えたタワーで漂白し、フローテーター(浮選機)でインク、灰分、ピッチ等の異物を浮上分離して、系外にフロスとして排出する。その後、パルプスラリーは、エキストラクタ等で水を除去し、更にパルプを水に再懸濁した後、フィルターでパルプを洗浄して脱墨パルプ(DIP)を得ることができる。本発明の異物除去剤は、フローテーターに添加してもよく、又はその前段階で添加してもよいが、フローテーター直前に添加することが好ましい。
フローテーターでは、パルプスラリーに気泡を吹き込み、泡にインク等の異物を付着させて浮上させ、パルプと分離する。この場合、公知の有機脱墨剤を添加することもできる。
従来技術においては、この状態でフローテーションを行っても、剥離したインク等の異物は分散状態に保たれて分離しにくいが、本発明に係る前記カチオン性単独重合体又は共重合体を添加してフローテーションを行うと、剥離したインク、ピッチ、灰分等の異物が凝集してフロックを形成し、これが気泡に付着して浮上し分離される。このようにしてパルプスラリーのインク、灰分、ピッチ等の異物の除去率が向上すると、得られた脱墨パルプを配合して製造した紙製品の白色度の向上や、異物による欠点、断紙の低減、歩留り、ろ水性の向上、紙強度の向上等の品質改善や、生産性の向上、操業性の改善に繋がる。また、これらの改善点により、脱墨パルプの配合率を高めることができ、製造原価に占めるパルプ原料費を低減することが可能となる。
(Specific production example of deinked pulp)
Production of deinked pulp in the present invention can be carried out in the same manner as conventionally known deinked pulp production methods. For example, first, waste paper is added to water containing alkali such as sodium hydroxide and sodium silicate, the used paper is disaggregated with a pulper (pulp disaggregation device) to make a pulp slurry, and then a pulp slurry and a deinking agent (for example, a kneader) Nonionic surfactant) is kneaded and the printing ink is peeled off from the pulp. Next, the mixture is bleached with a tower to which hydrogen peroxide has been added, and foreign matters such as ink, ash, and pitch are floated and separated by a flotator (flotation machine) and discharged out of the system as floss. Thereafter, the pulp slurry can be deinked pulp (DIP) by removing water with an extractor or the like and further resuspending the pulp in water and then washing the pulp with a filter. The foreign matter removing agent of the present invention may be added to the flotator or may be added at the previous stage, but is preferably added immediately before the flotator.
In the flotator, bubbles are blown into the pulp slurry, and foreign matters such as ink are attached to the bubbles to float and separate from the pulp. In this case, a known organic deinking agent can also be added.
In the prior art, even if flotation is performed in this state, foreign matter such as peeled ink is kept in a dispersed state and difficult to separate, but the cationic homopolymer or copolymer according to the present invention is added. When flotation is performed, foreign matter such as separated ink, pitch, and ash aggregates to form a flock, which adheres to bubbles and floats and is separated. Thus, when the removal rate of foreign matter such as ink, ash, and pitch of the pulp slurry is improved, the whiteness of the paper product produced by blending the obtained deinked pulp is improved, and the defects due to foreign matter, This leads to quality improvements such as reduction, yield, freeness improvement, and paper strength improvement, productivity improvement, and operability improvement. In addition, these improvements make it possible to increase the blending ratio of deinked pulp, and to reduce the pulp raw material cost in the manufacturing cost.

このようにしてインク、ピッチ、灰分等の異物が除去された脱墨パルプは、新聞紙、雑誌紙、OA紙、中質印刷紙、チラシ紙、段ボール紙等を製造する古紙原料として、好適に使用することができる。   The deinked pulp from which foreign matters such as ink, pitch and ash are removed in this way is suitably used as a waste paper material for producing newspaper, magazine paper, OA paper, medium-size printing paper, flyer paper, cardboard paper, etc. can do.

次に、本発明を実施例により更に詳細に説明するが、本発明はこれらの例によってなんら限定されるものではない。
なお、フロス量、スラリーの懸濁固形分濃度、ピッチ濃度、及びパルプシートの白色度の測定は以下の方法により行った。
(1)フロス量
パルプスラリーをフローテーターにより処理して、インク等の異物を浮上分離して、系外にフロスとして排出した量を測定した。
(2)スラリーの懸濁固形分濃度
JIS K 0l02に準じて、フローテーション処理後のパルプスラリーの懸濁固形分濃度を測定した。
(3)スラリーのピッチ濃度
フローテーション処理後に採取したパルプスラリーを蒸発乾固し、ジクロロメタンを用いてソックスレー抽出を行い、抽出重量からピッチ(パルプ中に混入した接着剤や合成樹脂等)の濃度を算出した。
(4)パルプシートの白色度
タッピシートマシンを用いて、JIS P 8209に準じてパルプシート2枚を作製し、得られたパルプシートについて、ハンター白色度計を用いて、JIS P 8123に準じて白色度を測定した。白色度は、各シートにつき5点測定し、その平均値を求めた。
なお、白色度は32以上が好ましい。
EXAMPLES Next, although an Example demonstrates this invention still in detail, this invention is not limited at all by these examples.
In addition, the measurement of the amount of froth, the suspended solid content concentration of a slurry, pitch concentration, and the whiteness of a pulp sheet was performed with the following method.
(1) Floss amount The pulp slurry was treated with a floatator to float and separate foreign substances such as ink, and the amount discharged as floss out of the system was measured.
(2) Suspension solid content concentration of slurry The suspension solid content concentration of the pulp slurry after the flotation treatment was measured according to JIS K 0102.
(3) Pitch concentration of the slurry The pulp slurry collected after the flotation treatment is evaporated to dryness, soxhlet extraction is performed using dichloromethane, and the concentration of pitch (adhesive or synthetic resin mixed in the pulp) is determined from the extracted weight. Calculated.
(4) Whiteness of pulp sheet Using a tapi sheet machine, two pulp sheets were prepared in accordance with JIS P 8209, and the obtained pulp sheet was in accordance with JIS P 8123 using a hunter whiteness meter. The whiteness was measured. The whiteness was measured at five points for each sheet, and the average value was obtained.
The whiteness is preferably 32 or more.

製造例1
ジメチルアミノプロピルアクリルアミド塩化メチル4級塩(興人株式会社製、DMAPAA−Q、79%水溶液、粘度80〜90cps(25℃))とジメチルアクリルアミド(和光純薬工業株式会社製、活性アルミナを用いて重合禁止剤を取り除いてから使用)とを25℃で反応させ、ジメチルアミノプロピルアクリルアミド塩化メチル4級塩:ジメチルアクリルアミド(モル比)=99:1の共重合体(重量平均分子量:20万)を得た。
結果を表1に示す。
製造例2
ジアリルジメチルアンモニウムクロリド(60%水溶液)とジメチルアクリルアミド(和光純薬工業株式会社製、活性アルミナを用いて重合禁止剤を取り除いてから使用)とを25℃で反応させ、ジアリルジメチルアンモニウムクロリド:ジメチルアクリルアミド(モル比)=30:70の共重合体(重量平均分子量:300万)を得た。
結果を表1に示す。
Production Example 1
Using dimethylaminopropylacrylamide methyl chloride quaternary salt (manufactured by Kojin Co., Ltd., DMAPAA-Q, 79% aqueous solution, viscosity 80-90 cps (25 ° C.)) and dimethylacrylamide (manufactured by Wako Pure Chemical Industries, Ltd., activated alumina) And used after removing the polymerization inhibitor) at 25 ° C., and a dimethylaminopropylacrylamide methyl chloride quaternary salt: dimethylacrylamide (molar ratio) = 99: 1 copolymer (weight average molecular weight: 200,000). Obtained.
The results are shown in Table 1.
Production Example 2
Diallyldimethylammonium chloride (60% aqueous solution) and dimethylacrylamide (manufactured by Wako Pure Chemical Industries, Ltd., used after removing the polymerization inhibitor using activated alumina) are reacted at 25 ° C., and diallyldimethylammonium chloride: dimethylacrylamide A copolymer (molar ratio) = 30: 70 (weight average molecular weight: 3 million) was obtained.
The results are shown in Table 1.

製造例3
ヘキサメチレンジアミン2.36gに脱塩水11gを加え、40重量%ジメチルアミン水溶液70.5g(有効分28.2g)を更に加え、ヘキサメチレンジアミンを溶解させた。エピクロルヒドリン64.8gを滴下ロートに入れ、17〜18℃に保ちつつ、得られたヘキサメチレンジアミン溶液に6時間かけて滴下して反応させた。
得られた反応液を50℃に加熱し、3時間保持した後、90℃まで昇温し、33重量%水酸化ナトリウム水溶液2.4mLを加え、更に90℃で3時間保持し、その後水溶液を30℃まで冷却した。次いで、6N塩酸を加えて水溶液のpHを5.5に調整し、エピクロルヒドリン・ジメチルアミン縮合物(重量平均分子量:25万)を得た。
結果を表1に示す。
Production Example 3
11 g of demineralized water was added to 2.36 g of hexamethylene diamine, and 70.5 g (effective amount 28.2 g) of a 40 wt% dimethylamine aqueous solution was further added to dissolve hexamethylene diamine. Epichlorohydrin 64.8g was put into the dropping funnel and it was made to react by dripping over 6 hours to the obtained hexamethylenediamine solution, keeping at 17-18 degreeC.
The obtained reaction solution was heated to 50 ° C. and held for 3 hours, and then heated to 90 ° C., 2.4 mL of 33 wt% sodium hydroxide aqueous solution was added, and further maintained at 90 ° C. for 3 hours. Cooled to 30 ° C. Subsequently, 6N hydrochloric acid was added to adjust the pH of the aqueous solution to 5.5 to obtain an epichlorohydrin-dimethylamine condensate (weight average molecular weight: 250,000).
The results are shown in Table 1.

Figure 0005593791
Figure 0005593791

実施例1及び2
新聞及びチラシを古紙原料として脱墨処理を行っている古紙パルプ製造工程において、2次フローテーター(1次フローテーターのフロス処理用フローテーター)の原水を試料に用いた。
上記試料5Lと、製造例1で得られた(ジメチルアミノプロピルアクリルアミド塩化メチル4級塩/ジメチルアクリルアミド)の共重合体を表2に示す量で添加し、小型MTフローテーター(株式会社IHI機械システム製)に入れ、30秒間撹拌した。
次に、空気量を3L/minに設定し、4分間のフローテーション処理を行った。
結果を表2に示す。
Examples 1 and 2
In the waste paper pulp manufacturing process in which deinking processing is performed using newspapers and flyers as raw paper raw materials, raw water of a secondary flowator (a flowmeter for froth treatment of a primary flowator) was used as a sample.
The sample 5L and the copolymer of (dimethylaminopropylacrylamide methyl chloride quaternary salt / dimethylacrylamide) obtained in Production Example 1 were added in the amounts shown in Table 2, and a small MT flowator (IHI Mechanical System Co., Ltd.) was added. And stirred for 30 seconds.
Next, the amount of air was set to 3 L / min, and a 4 minute flotation process was performed.
The results are shown in Table 2.

比較例1〜3
実施例1において、異物除去剤として、製造例2で得られた(ジアリルジメチルアンモニウムクロリド/ジメチルアクリルアミド)の共重合体を表2に示す量で添加した以外は、実施例1と同様の操作を行った。結果を表2に示す。
比較例4〜5
実施例1において、異物除去剤として、製造例3で得られたエピクロルヒドリン・ジメチルアミン縮合物を表2に示す量で添加した以外は、実施例1と同様の操作を行った。結果を表2に示す。
Comparative Examples 1-3
In Example 1, the same operation as in Example 1 was performed except that the copolymer of (diallyldimethylammonium chloride / dimethylacrylamide) obtained in Production Example 2 was added in the amount shown in Table 2 as a foreign substance removing agent. went. The results are shown in Table 2.
Comparative Examples 4-5
In Example 1, the same operation as in Example 1 was performed, except that the epichlorohydrin-dimethylamine condensate obtained in Production Example 3 was added in the amount shown in Table 2 as a foreign substance removing agent. The results are shown in Table 2.

Figure 0005593791
Figure 0005593791

実施例1及び2では、スラリー中のピッチ濃度が低く、白色度が高いパルプシートが得られた。これに対し、比較例1(異物除去剤無添加)、比較例2〜3(DADMAC系共重合体を添加)においては、スラリー中のピッチ濃度が高く、白色度は低い結果であった。
また、比較例4及び5(エピクロルヒドリン・ジメチルアミン縮合物を添加)においては、白色度については実施例とほぼ同等の結果が得られたものの、スラリー中のピッチ濃度は実施例の結果には及ばなかった。
In Examples 1 and 2, pulp sheets with low pitch concentration and high whiteness in the slurry were obtained. On the other hand, in Comparative Example 1 (no foreign substance removing agent added) and Comparative Examples 2 to 3 (DADMAC type copolymer added), the pitch concentration in the slurry was high and the whiteness was low.
Further, in Comparative Examples 4 and 5 (with epichlorohydrin / dimethylamine condensate added), although the results of whiteness were almost the same as those of the examples, the pitch concentration in the slurry reached the results of the examples. There wasn't.

本発明の異物除去剤、異物除去方法、及び脱墨パルプの製造方法によれば、パルプ繊維の歩留り低下を最小限に抑えながら効率的にコロイド粒子を凝集させ、フローテーターでのインク、灰分、ピッチ等の異物除去を効率的に行うことができる。また、本発明の異物除去剤、異物除去方法、及び脱墨パルプの製造方法は、高いpH環境下や、高塩類環境下における古紙処理においても有効である。   According to the foreign matter removing agent, foreign matter removing method, and deinked pulp manufacturing method of the present invention, colloidal particles are efficiently agglomerated while minimizing a decrease in the yield of pulp fibers, and ink, ash content in a flowmeter, Foreign matter such as pitch can be removed efficiently. The foreign matter removing agent, the foreign matter removing method, and the deinked pulp manufacturing method of the present invention are also effective in used paper processing under a high pH environment or a high salt environment.

Claims (4)

下記一般式(1)で表される第四級アンモニウム基含有モノマー由来の構成単位を有するカチオン性共重合体を含有する脱墨工程におけるフローテーター用異物除去剤であって、
前記共重合体における、前記一般式(1)で表される第四級アンモニウム基含有モノマーと共重合する共重合モノマーは、無置換又は炭素数1〜5の直鎖又は分岐鎖のアルキル基により置換されたアクリルアミド及び/又はメタクリルアミドであり、
前記共重合体は、前記アクリルアミド及び/又はメタクリルアミド由来の構成単位を30モル%以下含有する、フローテーター用異物除去剤。
Figure 0005593791
(式中、R1及びR2は水素原子又はメチル基を示し、R3及びR4は水素、炭素数1〜4のアルキル基、ピペラジン基、ピペリジン基又はモルホリン基を示し、R5は炭素数1〜22の炭化水素基を示し、Aは炭素数1〜5のアルカンジイル基を示し、Xは第四級アンモニウム基の対イオンを示す。)
A foreign matter removing agent for flotation in deinking process comprising a cationic copolymer having a constitutional unit derived from the quaternary ammonium group-containing monomer represented by the following general formula (1),
The copolymerizable monomer that is copolymerized with the quaternary ammonium group-containing monomer represented by the general formula (1) in the copolymer is an unsubstituted or linear or branched alkyl group having 1 to 5 carbon atoms. Substituted acrylamide and / or methacrylamide;
The copolymer is a foreign matter removing agent for a floatator, containing 30 mol% or less of the structural unit derived from the acrylamide and / or methacrylamide.
Figure 0005593791
(Wherein R 1 and R 2 represent a hydrogen atom or a methyl group, R 3 and R 4 represent hydrogen, an alkyl group having 1 to 4 carbon atoms, a piperazine group, a piperidine group or a morpholine group, and R 5 represents a carbon atom. (A represents a C 1-5 alkanediyl group, and X represents a counter ion of a quaternary ammonium group.)
カチオン性共重合体の重量平均分子量が10万〜200万である、請求項1に記載のフローテーター用異物除去剤。 The weight average molecular weight of the cationic copolymer is 100,000 2,000,000 flotation for foreign matter removal agent according to claim 1. 請求項1又は2に記載の異物除去剤を、古紙の脱墨処理におけるフローテーション工程又はその前工程に添加することを特徴とする異物除去方法。   A foreign matter removing method, wherein the foreign matter removing agent according to claim 1 or 2 is added to a flotation step or a preceding step in a deinking process of waste paper. 脱墨工程のパルプスラリー中に、下記一般式(1)で表される第四級アンモニウム基含有モノマー由来の構成単位を有するカチオン性共重合体を添加する脱墨パルプの製造方法であって、
前記共重合体における、前記一般式(1)で表される第四級アンモニウム基含有モノマーと共重合する共重合モノマーは、無置換又は炭素数1〜5の直鎖又は分岐鎖のアルキル基により置換されたアクリルアミド及び/又はメタクリルアミドであり、
前記共重合体は、前記アクリルアミド及び/又はメタクリルアミド由来の構成単位を30モル%以下含有する、脱墨パルプの製造方法。
Figure 0005593791
(式中、R1及びR2は水素原子又はメチル基を示し、R3及びR4は水素、炭素数1〜4のアルキル基、ピペラジン基、ピペリジン基又はモルホリン基を示し、R5は炭素数1〜22の炭化水素基を示し、Aは炭素数1〜5のアルカンジイル基を示し、Xは第四級アンモニウム基の対イオンを示す。)
To the pulp slurry during the deinking process, a process for the preparation of a deinked pulp of adding a cationic copolymer having a constitutional unit derived from the quaternary ammonium group-containing monomer represented by the following general formula (1),
The copolymerizable monomer that is copolymerized with the quaternary ammonium group-containing monomer represented by the general formula (1) in the copolymer is an unsubstituted or linear or branched alkyl group having 1 to 5 carbon atoms. Substituted acrylamide and / or methacrylamide;
The method for producing deinked pulp, wherein the copolymer contains 30 mol% or less of the structural unit derived from the acrylamide and / or methacrylamide.
Figure 0005593791
(Wherein R 1 and R 2 represent a hydrogen atom or a methyl group, R 3 and R 4 represent hydrogen, an alkyl group having 1 to 4 carbon atoms, a piperazine group, a piperidine group or a morpholine group, and R 5 represents a carbon atom. (A represents a C 1-5 alkanediyl group, and X represents a counter ion of a quaternary ammonium group.)
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