JP2645208B2 - Deinking agent for recycled paper - Google Patents
Deinking agent for recycled paperInfo
- Publication number
- JP2645208B2 JP2645208B2 JP16920693A JP16920693A JP2645208B2 JP 2645208 B2 JP2645208 B2 JP 2645208B2 JP 16920693 A JP16920693 A JP 16920693A JP 16920693 A JP16920693 A JP 16920693A JP 2645208 B2 JP2645208 B2 JP 2645208B2
- Authority
- JP
- Japan
- Prior art keywords
- deinking agent
- ink
- deinking
- paper
- foam
- 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
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
Landscapes
- Paper (AREA)
Description
【0001】[0001]
【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
誌等をフローテーション法で脱墨処理するに際し、高白
色度で残インキ数の少ない脱墨パルプが得られ、かつ起
泡力をある程度維持しつつ消泡性に優れた脱墨剤に関す
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a deinking agent used for recycling used paper such as newspapers and magazines. More specifically, when deinking newspapers, magazines, etc. by the flotation method, deinked pulp with high whiteness and a small number of remaining inks can be obtained. About black ink.
【0002】[0002]
【従来の技術及び発明が解決しようとする課題】従来、
脱墨剤として、例えばポリエチレンアルキルエーテルな
どは、古紙からのインキ剥離、フローテーションシステ
ムで要求されるところのインキ除去性、起泡力等、必要
不可欠の機能をすべて併せもっているところから広く使
用されている。しかしながら、近年の再生紙ユーザーの
要求品質の高度化、さらには、回収古紙に使用されてい
るインキの多様化等、今日において従来の脱墨剤では、
対応できない様々な状況変化が生じている。2. Description of the Related Art
As a deinking agent, for example, polyethylene alkyl ether is widely used because it has all the essential functions such as ink removal from waste paper, ink removal and foaming power required by flotation systems. ing. However, today's conventional deinking agents, such as the sophistication of the required quality of recycled paper users and the diversification of ink used in recovered waste paper,
There are various situations that cannot be dealt with.
【0003】例えば、夏場長期にわたって野ざらしにさ
れた原料にみられる様な熱劣化した古紙を脱墨工程で処
理すると、最終製品に残るインキ量が増大するというト
ラブルが生じる。その原因として、熱や酸素によってイ
ンキが変質し、インキと紙の結着が強固になると考えら
れている。この様な熱劣化古紙は、従来の脱墨剤ではま
ったく効果があがらず、やむなく他の化学薬品の増量高
せん断システムへの変換など、きわめて高コストな対応
にせまられる。For example, when a waste paper that has been thermally degraded, such as that found in raw materials exposed for a long period of time in summer, is treated in the deinking process, a problem occurs in that the amount of ink remaining in the final product increases. As a cause, it is considered that the quality of the ink is changed by heat or oxygen, and the binding between the ink and the paper is strengthened. Such heat-degraded waste paper is ineffective at all with conventional deinking agents, and is inevitably costly, such as converting other chemicals into increased-shear systems.
【0004】又、近年の工場の水使用システムは、環境
対策あるいはランニングコストの低下等の目的にあわ
せ、循環水を用いるクローズド化が主流となっている。
脱墨工程水のクローズド化が強化されると、原料由来の
インキ、塗料、あるいは工程薬剤由来の化学薬品が、回
収水中から工程内に流れ込む。特に、脱墨剤が循環水を
通して工程内をリサイクルすると、そのものの起泡力が
必要以上に大きくなり、フローテーションでの排水ピッ
トでの泡トラブルを起こす。さらに抄紙工程に、残存泡
が発生すると、スラリー中の泡が脱水をさまたげること
になり、ろ水性が悪化し、最悪の場合、紙ぎれを起こ
す。[0004] In recent years, the water use system of factories has been mainly closed using circulating water for the purpose of environmental measures or reduction of running cost.
When the closed state of the deinking process water is strengthened, inks, paints, or chemicals derived from process chemicals from the raw materials flow into the process from the recovered water. In particular, when the deinking agent is recycled in the process through the circulating water, the foaming power of the process itself becomes larger than necessary, causing foam trouble in the drainage pit in flotation. Further, when residual foam is generated in the papermaking process, foam in the slurry impedes dehydration, resulting in poor drainage and, in the worst case, paper breakage.
【0005】[0005]
【課題を解決するための手段】本発明者等は、この様な
背景に鑑み、鋭意研究の結果、特定の3成分を用いるこ
とにより、紙−インキ間への浸透性、インキ除去性及び
起泡性をある程度維持しつつ、起泡した泡はすみやかに
破泡する様、消泡性を強化し、本発明の脱墨剤を完成す
るに至った。Means for Solving the Problems In view of such a background, the present inventors have conducted intensive studies and as a result, have found that by using specific three components, the permeability between paper and ink, ink removability and ink removal properties can be improved. While maintaining the foaming properties to some extent, the foamed foams were quickly broken to enhance the defoaming properties, thereby completing the deinking agent of the present invention.
【0006】即ち、本発明は、下記の一般式 (A) 、
(B) 、 (C) で表される化合物を含有する脱墨剤であ
って、一般式 (A) 、 (B) 、 (C) で表される化合物
において、 -(AO) l - 、 -(AO) m - 及び -(AO) n -鎖中に
は、エチレンオキサイド重合物の存在が必須条件で、全
アルキレンオキサイド重合物中におけるエチレンオキサ
イド重合物の割合は30〜80モル%であり、かつ一般式
(A) 、 (B) 、 (C) で表される化合物の重量比が、
(A) : (B) : (C) =20〜40:30〜70:20〜40であ
ることを特徴とする脱墨剤に関する。That is, the present invention provides the following general formula (A):
A deinking agent containing the compounds represented by (B) and (C).
Thus, compounds represented by general formulas (A), (B) and (C)
In the-(AO) l -,-(AO) m- and- (AO) n -chains
Is an essential condition that the presence of ethylene oxide polymer
Ethylene oxa in alkylene oxide polymer
The proportion of the polymer is 30 to 80 mol%, and the general formula
The weight ratio of the compounds represented by (A), (B) and (C) is
(A): (B): (C) = 20-40: 30-70: 20-40
That relates to a deinking agent, characterized in that.
【0007】 (式中、R1,R2,R3;炭素数8〜24のアルキル基又はアル
ケニル基の中から選ばれる基 AO;炭素数2〜4のオキシアルキレン基 l,m,n ;10〜100 の整数 を示す。)[0007] (Wherein, R 1 , R 2 , R 3 ; a group AO selected from an alkyl group or an alkenyl group having 8 to 24 carbon atoms; an oxyalkylene group l, m, n having 2 to 4 carbon atoms; 10 to 100) Indicates the integer of.)
【0008】特公昭64-11756号公報では、上記の一般式
(A) 、 (B) で表される化合物 (以下それぞれA成
分、B成分と称す) を含有する脱墨剤が記載されている
が、これら2成分だけでは消泡性に劣るため、前述の問
題点を有するものであった。しかしながら、本発明では
一般式 (C) で表される化合物 (以下C成分と称す) を
新たに加えることによって、はじめて上記の浸透、消泡
力強化効果が向上することを見出した。In Japanese Patent Publication No. 64-11756, the general formula
A deinking agent containing the compounds represented by (A) and (B) (hereinafter referred to as A component and B component, respectively) is described. It had problems. However, in the present invention, it has been found that the above-mentioned effect of enhancing penetration and defoaming power is improved only by newly adding a compound represented by the general formula (C) (hereinafter, referred to as component C).
【0009】A、B、C成分の重量比は、A成分:B成
分:C成分=20〜40:30〜70:20〜40である。The weight ratio of the A, B, and C components is A component: B component: C component = 20-40: 30-70: 20-40.
【0010】A、B成分においてR1〜R3は炭素数8〜24
のアルキル基又はアルケニル基の中から選ばれる基であ
るが、炭素数が24を越えると十分な起泡力が得られず、
フローテーションでの泡立ちが不足し、インキ除去が不
充分となる。又、パルプとの親和性が不足することから
インキ−紙間の浸透性が不足する。炭素数が8に満たな
い場合は、インキとの親和性が低い為、インキを捕集除
去しきれず、くすみのあるパルプしか得ることができな
い。In the components A and B, R 1 to R 3 have 8 to 24 carbon atoms.
Is a group selected from among alkyl groups or alkenyl groups, but if the carbon number exceeds 24, sufficient foaming power cannot be obtained,
Insufficient foaming in flotation and insufficient ink removal. In addition, since the affinity with pulp is insufficient, the permeability between ink and paper is insufficient. When the number of carbon atoms is less than 8, the affinity with the ink is low, so that the ink cannot be completely collected and removed, and only a dull pulp can be obtained.
【0011】A、B、C成分においてAOは炭素数2〜4
のアルキレンオキサイド重合物であるが、-(AO) l- 、
-(AO)m- 、及び -(AO)n-重合鎖にはエチレンオキサイド
は必須であり、全アルキレンオキサイド重合物に占める
割合は30〜80モル%である。アルキレンオキサイド重合
鎖中のエチレンオキサイド、プロピレンオキサイド等は
ブロック重合でもランダム重合でもよく、エチレンオキ
サイドはインキと紙との剥離性を強化する為に必要であ
る。また、l,m,nの各モル数が10〜100 モルの範囲
にあると、インキ−紙間の浸透性が向上し、小さな機械
力で容易にインキが剥離する。l,m,nの各モル数が
この範囲を越えるとフローテーションでのインキ除去効
果が低下したり泡トラブルを起こす要因を内在する。In the components A, B and C, AO has 2 to 4 carbon atoms.
Alkylene oxide polymer of-(AO) l- ,
Ethylene oxide is essential for the-(AO) m- and-(AO) n -polymer chains, and the proportion of the total alkylene oxide polymer is 30 to 80 mol% . Ethylene oxide in the A Ruki alkylene oxide polymer chain, propylene oxide may be a random polymer in block polymerization, ethylene oxide is required in order to enhance the releasability of the ink and paper. When the number of moles of 1, m and n is in the range of 10 to 100 moles, the permeability between the ink and the paper is improved, and the ink is easily peeled off with a small mechanical force. If the moles of 1, m, and n exceed this range, there are inherent factors that reduce the ink removing effect in flotation and cause bubble trouble.
【0012】上記条件を満たしたC成分は、起泡・消泡
をコントロールする上で重要な因子となる。特にnが10
〜100 モルの範囲にあると十分な起泡力と同時に起泡し
た泡は速やかに消泡し、フローテーション工程での泡に
関する操作性を著しく改善することができる。具体的に
は、フローテーションから排出されるフロスの泡は、す
みやかに消泡され、クローズド化によって蓄積し、抄紙
工程に脱墨剤が流れ込むことがあっても泡立つことがな
く、過剰発泡や紙切れ等のトラブルを解消する。The C component satisfying the above conditions is an important factor in controlling foaming and defoaming. Especially n is 10
When the amount is within the range of 100 to 100 mol, the foam generated at the same time as the sufficient foaming power is quickly eliminated, and the operability of the foam in the flotation step can be remarkably improved. Specifically, the floss foam discharged from the flotation is quickly defoamed, accumulates due to closing, and does not foam even if the deinking agent flows into the papermaking process, resulting in excessive foaming and paper breakage. Eliminate troubles such as
【0013】従ってC成分の構造を決定するnとエチレ
ンオキサイドの割合が適切な範囲に制御されていると脱
墨性の中での泡に関する操作性を従来の脱墨剤と比較し
て卓越したレベルに向上させる。Therefore, when the ratio of n and ethylene oxide, which determine the structure of the component C, is controlled within an appropriate range, the operability of the foam in the deinking property is excellent as compared with the conventional deinking agent. Improve to the level.
【0014】A、B成分は、例えば、アルキレンオキシ
ドを付加させた重合物に脂肪酸を反応させ、エステル化
反応を行うか、または脂肪酸にアルキレンオキシドを付
加反応させることによって得ることができる。具体的な
脂肪酸としては、カプリン酸、ラウリン酸、ミリスチン
酸、パルミチン酸、ステアリン酸、オレイン酸、リノー
ル酸、ベヘニン酸等、及びそれらの脂肪酸を含むヤシ油
脂肪酸、大豆脂肪酸、トール油脂肪酸、牛脂脂肪酸、魚
油脂肪酸等、またはそれら脂肪酸の水素添加物の天然物
より得られる脂肪酸及び合成脂肪酸等が用い得る。The components A and B can be obtained, for example, by reacting a polymer to which an alkylene oxide has been added with a fatty acid and performing an esterification reaction, or by subjecting the fatty acid to an addition reaction with the alkylene oxide. Specific fatty acids include capric acid, lauric acid, myristic acid, palmitic acid, stearic acid, oleic acid, linoleic acid, behenic acid, etc., and coconut oil fatty acids, soybean fatty acids, tall oil fatty acids, tallow oil, and tallow oil containing those fatty acids. Fatty acids, fish oil fatty acids, and the like, or fatty acids and synthetic fatty acids obtained from hydrogenated natural products of these fatty acids can be used.
【0015】本発明の脱墨剤の添加量は原料古紙に対し
て 0.2〜1.0 重量%が好ましい。また、本発明の脱墨剤
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
とも可能である。The amount of the deinking agent of the present invention is preferably from 0.2 to 1.0% by weight based on the raw waste paper. Further, the deinking agent of the present invention can be used in combination with a known deinking agent generally used conventionally.
【0016】[0016]
【実施例】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。EXAMPLES The present invention will be described below in detail with reference to examples, but the present invention is not limited to these examples.
【0017】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、CaCl2(対原
料)1.0%を添加し、30℃にて10分間フローテーション処
理を施した。フロー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、スタ
ンダード TAPPI沙紙機にてパルプシートを作製した。得
られたパルプシートを側色色差計にて白色度を測定、画
像解析装置 (×126倍) にて残インキ数を測定した。Example 1 A used newspaper collected in the city was shredded to 2 × 5 cm, and a certain amount was put into a tabletop disintegrator, in which water and caustic soda (based on raw material)
1.0% (weight basis, the same applies hereinafter), sodium silicate (based on raw material) 3.
0%, 30% hydrogen peroxide (based on raw material) 3.0%, various deinking agents shown in Table 1 (based on raw material) 0.4%, pulp concentration 5%, 55%
After separating at 20 ° C. for 20 minutes, the mixture was aged at 50 ° C. for 60 minutes. Thereafter, water was added to dilute the pulp concentration to 1.0%, 1.0% of CaCl 2 (based on raw material) was added, and a flotation treatment was performed at 30 ° C. for 10 minutes. 6 pulp slurry after flotation
After concentration to a concentration of 1%, water was added to dilute the solution to a concentration of 1%, and a pulp sheet was prepared using a standard TAPPI Sagami machine. The whiteness of the obtained pulp sheet was measured with a side colorimeter, and the number of remaining inks was measured with an image analyzer (× 126).
【0018】破泡試験及びろ水試験については下記のよ
うに行った。 ・破泡試験 1.ラボフローテーターで1%スラリーを処理する 2.排出された泡を採取する 3.一定量(約50cc)の排出液にバブルストーンを 200cc
栓付きメスフラスコに沈める 4.一定量の空気を通す 5.気泡の高さが一定になったことを確認して通気を止め
る 6.その時の泡高を測定する(H0 cm) 7. 60s間破泡の様子を観察する 8. 60s後の泡高を測定する(H60 cm) 9.破泡率は下式により表される。The foam breaking test and the drainage test were performed as follows.・ Bubble breaking test 1. Treat 1% slurry with a lab floatator 2. Collect the discharged foam 3. 200cc of bubble stone in a certain amount (about 50cc) of the discharged liquid
Submerge in a volumetric flask with a stopper. 4. Pass a certain amount of air. 5. Confirm that the height of the bubbles has become constant, and stop the ventilation. 6. Measure the bubble height at that time (H 0 cm). 7. 60s Observe the state of foam breaking 8. Measure the foam height after 60 s (H 60 cm) 9. The foam breaking rate is expressed by the following formula.
【0019】[0019]
【数1】 (Equation 1)
【0020】・ろ水性試験 1.パルプスラリー 1.5%、300ml をスタンダード TAPPI
沙紙機に加える 2.スタンダードTAPPI 抄紙機に一定量加水し、中のスラ
リーを攪拌均一化する 3.脱水を開始し、スラリーがシート化するまでの時間を
測定する 4.シート化するに至る時間が短い程、ろ水性は良いと判
断する。・ Water drainage test 1. Pulp slurry 1.5%, 300ml is standard TAPPI
Add to paper machine 2. Standard TAPPI Add a certain amount of water to paper machine and stir and equalize slurry inside 3. Start dewatering and measure time until slurry turns into sheet 4. Lead to sheet The shorter the time, the better the drainage.
【0021】以上の結果を併せて表1に示す。Table 1 also shows the above results.
【0022】[0022]
【表1】 [Table 1]
【0023】注) ・No.3, No.4のR1, R2, R3はオレイン酸由来のアルキル
基 ・ -(EO)x(PO)y- はアルキル基方向からEO, POの順でx
モル、yモルをブロック付加 ・ -(EO/POx/y)-はxモル、yモルの混合比でランダム
付加 ・成分A R1COO(AO)lCOR2 ・成分B R3COO(AO)mH ・成分C HO(AO)nHNote) ・ R 1 , R 2 and R 3 of No. 3 and No. 4 are alkyl groups derived from oleic acid ・-(EO) x (PO) y -is EO and PO in the direction of the alkyl group And x
Addition of moles and y moles--(EO / PO x / y )-is a random addition at a mixing ratio of x moles and y moles-Component A R 1 COO (AO) l COR 2 · Component B R 3 COO (AO ) m H · Component C HO (AO) n H
Claims (1)
表される化合物を含有する脱墨剤であって、一般式
(A) 、 (B) 、 (C) で表される化合物において、 -
(AO) l - 、 -(AO) m - 及び -(AO) n -鎖中には、エチレンオ
キサイド重合物の存在が必須条件で、全アルキレンオキ
サイド重合物中におけるエチレンオキサイド重合物の割
合は30〜80モル%であり、かつ一般式 (A) 、 (B) 、
(C) で表される化合物の重量比が、 (A) : (B) :
(C) =20〜40:30〜70:20〜40であることを特徴とす
る脱墨剤。 (式中、R1,R2,R3;炭素数8〜24のアルキル基又はアル
ケニル基の中から選ばれる基 AO;炭素数2〜4のオキシアルキレン基 l,m,n ;10〜100 の整数 を示す。)1. A deinking agent containing a compound represented by the following general formulas (A), (B) and (C):
In the compounds represented by (A), (B) and (C),-
(AO) l -,-(AO) m- and- (AO) n-
The essential condition is that the oxide polymer is present.
Ethylene oxide polymer in side polymer
Is 30 to 80 mol%, and the general formulas (A), (B) and
The weight ratio of the compound represented by (C) is as follows: (A): (B):
(C) = 20 to 40:30 to 70:20 to 40, a deinking agent. (Wherein, R 1 , R 2 , R 3 ; a group AO selected from an alkyl group or an alkenyl group having 8 to 24 carbon atoms; an oxyalkylene group l, m, n having 2 to 4 carbon atoms; 10 to 100) Indicates the integer of.)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16920693A JP2645208B2 (en) | 1993-07-08 | 1993-07-08 | Deinking agent for recycled paper |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16920693A JP2645208B2 (en) | 1993-07-08 | 1993-07-08 | Deinking agent for recycled paper |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0726484A JPH0726484A (en) | 1995-01-27 |
JP2645208B2 true JP2645208B2 (en) | 1997-08-25 |
Family
ID=15882174
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16920693A Expired - Fee Related JP2645208B2 (en) | 1993-07-08 | 1993-07-08 | Deinking agent for recycled paper |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2645208B2 (en) |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5725489A (en) * | 1980-07-23 | 1982-02-10 | Nippon Oils & Fats Co Ltd | Deinking agent of used paper |
JPH084999B2 (en) * | 1987-07-07 | 1996-01-24 | トッキ株式会社 | Method and apparatus for polishing fine wire |
-
1993
- 1993-07-08 JP JP16920693A patent/JP2645208B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH0726484A (en) | 1995-01-27 |
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