JPH0541750B2 - - Google Patents
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- Publication number
- JPH0541750B2 JPH0541750B2 JP24633589A JP24633589A JPH0541750B2 JP H0541750 B2 JPH0541750 B2 JP H0541750B2 JP 24633589 A JP24633589 A JP 24633589A JP 24633589 A JP24633589 A JP 24633589A JP H0541750 B2 JPH0541750 B2 JP H0541750B2
- Authority
- JP
- Japan
- Prior art keywords
- pitch
- pulp
- control agent
- pitch control
- talc
- 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
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- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Paper (AREA)
Description
〔産業上の利用分野〕
本発明は、ピツチコントロール剤に関するもの
である。
〔従来の技術〕
パルプ、紙の製造工程におけるピツチトラブル
対策は古くからの重要課題である。
製紙工場においてピツチは、必然的に混入する
物質であり、主として木材チツプ、古紙パルプ、
ロジンサイズ剤等から持ち込まれ、一部排水とと
もに系外に除去されるもの、更に紙の中に抄き込
まれるもの以外は蒸解、叩解、抄紙の各工程内に
蓄積され、系内を循環している。
更に、各工程のパルプの処理設備、パルプスラ
リーの貯蔵チエストの壁、抄紙機上のワイヤー、
プレスロール、ドライヤーロール、毛布、カンバ
ス等に凝集したピツチ粒子が付着し、各種トラブ
ルを引き起こす。
従来の対策としては、例えば原料である木材
のシーズニングの強化、原料パルプの洗浄強
化、ピツチの少ない原料の選択、原料系:白
水系の発泡の抑制、界面活性剤、水溶性高分子
分散剤、澱粉、ゼラチン等の保護コロイド剤、エ
チレンジアミンテトラ酢酸(EDTA)、タルク等
のミキサーへの添加等の方法が採られている。
以上の他、従来珪藻土、シリカ、クレー、ベン
トナイト、酸性白土、タルク等をピツチ除去剤と
して、パルプ原料又は白水系に添加して用いるこ
とが知られている。
以上述べたピツチ除去剤は、いずれもピツチコ
ントロールの決め手になるものはなく、近年の原
料品質悪化に伴うピツチ増に対し、パルプ、古紙
パルプの製造工程及び製紙工程、白水処理工程の
ような様々な場所においてイオン性を有するピツ
チも含めて吸着できるほど効果的なピツチコント
ロール剤とはなつていない。
本発明者等は先に特開平1−104892号を以て新
しいピツチコントロール剤とピツチコントロール
方法を提案した。このピツチコントロール剤は酸
性白土の酸処理物とアルミニウム塩との反応2次
凝集物であつて、且つ吸油量が70ml/100g以上
で、比表面積が130m2/g以上という物性を有す
るものである。このピツチコントロール剤は酸性
白土の酸処理物をアルミニウム塩で処理してある
ため、水中における荷電したピツチ粒子の吸引力
を強め、大きな比表面積を利用してピツチコント
ロール効果を高めるものである。
しかしながら、このピツチコントロール剤もパ
ルプ製造工程、製紙工程に存在するすべてのピツ
チに対して万能ではなく、ある程度以上添加して
も効果が頭打ちとなり、たとえば、白水中に添加
した場合はおおむねピツチ除去率が50%程度以上
にすることは困難である。
〔発明が解決しようとする課題〕
以上のような現状から、原料の低品位化、古紙
の使用量の増加等増々ピツチが増える状況の中
で、パルプ製造工程、製指工程などいかなる場所
で使用しても種々のピツチに効果があり、なおか
つ、従来に比較してより高いピツチ除去率を有す
るピツチコントロール剤が要望されていた。
〔課題を解決するための手段〕
本発明は、酸性白土の酸処理物とアルミニウム
塩との反応2次凝集物であつて、かつ吸油量が80
ml/100g以上、比表面積が130m2/g以上で、更
に平均粒子径が2.7μ以上の前記反応2次凝集物と
平均粒径5μm以下のタルクとを、重量比で1:3
ないし3:1の割合で混合してなることを特徴と
するピツチコントロール剤である。
本発明のピツチコントロール剤が何故著効を現
わすかは明らかでないが、次のような理由が考え
られる。
すなわち、ピツチには、いくつかの種類があ
り、また、大きさの違いもあり、ピツチコントロ
ール剤の種類によつてはピツチへの吸着に選択性
があると考えられる。酸性白土の酸処理物とアル
ミニウム塩との反応2次凝集物とタルクでは吸着
するピツチの種類に差異があるものと思われる。
従つて、本発明のピツチコントロール剤を使用
した場合、各々のピツチコントロール剤が性質の
異なるピツチの吸着を分担し合い、より多くのピ
ツチをコントロールするものと考えられる。
本発明のピツチコントロール剤は、反応2次凝
集物とタルクの混合物であるが、その混合比率は
反応2次凝集物が多すぎても、また少なすぎても
反応2次凝集物の単独使用に比較してピツチ効果
の著効は得られず、反応2次凝集物のタルクの混
合比率は重量比で3:1〜1:3の割合とするこ
とを要する。本発明者等の実験よれば、混合比率
1:1のときに最も高いピツチ除去率が得られる
ことを確認している。
本発明のピツチコントロール剤は上記のように
各種の性質の異なるピツチを効率よく吸着し除去
するので、パルプ製造工程、製紙工程のあらゆる
個所へ効果的に使用できる。
パルプ製造工程、製紙工程の紙料中に添加する
場合は、パルプ(固形分)に対し、0.5〜3重量
%の使用で好ましいピツチ除去効果を得ることが
できる。
一方、本出願人がすでに特開平1−104892号公
報で提案したように、ピツチコントロール剤はピ
ツチが比較的少ないパルプ又は製紙工程の紙料中
に添加するよりも、ピツチが循環により蓄積し易
いパルプ製造工程、古紙パルプ製造工程及び製紙
工程を循環する白水中に添加する方が少量で効率
的に各種の性質の異なるピツチを除去できる。
各工程の白水中への添加場所及びその白水の使
用方法としては、例えば、抄紙工程の白水の紙料
回収設備で得られる高濃度白水へ本発明のピツチ
コントロール剤を添加すること、叩解したパルプ
の白水による稀釈に本発明のピツチコントロール
剤を添加した抄紙白水又は高濃度白水を使用する
こと、パルプ製造工程の循環白水及び古紙処理工
程の古紙循環白水に、本発明のピツチコントロー
ル剤を添加すること、並びに古紙脱インキ工程の
フローテーシヨン前の稀釈に本発明のピツチコン
トロール剤を添加した脱インキ最終工程で発生す
る白水を使用するなどが行われる。本発明のピツ
チコントロール剤によるピツチコントロール方法
は、これらを2個所以上並行して実施することに
より、抄紙した紙のピツチ斑点及び各工程のピツ
チトラブルのコントロールに著しい効果をあげる
ことができる。
本発明のピツチコントロール剤である酸性白土
の酸処理物(活性白土)とアルミニウム塩との反
応2次凝集物とタルクとの混合物の上記各工程の
白水への添加量は、白水固形分(パルプ)に対
し、0.1〜3重量%で充分効果を発揮する。実際
には工程によつて添加量は異なり、たとえばパル
プ工程では0.1〜0.5重量%、古紙処理工程では0.2
〜1重量%で好ましい除去効果が得られる。ま
た、本発明のピツチコントロール剤を白水に適用
する場合は白水中の紙料分に対して0.1〜3重量
%添加するので、その使用量はパルプ又は紙料固
形分に対して白水を固形分として15%使用すると
してパルプ又は紙料の繊維分に対しては0.014〜
0.45重量%になり、通常のパルプ原料に添加する
ピツチコントロール剤の使用量に比べて、1/10程
度でピツチコントロール効果をあげることができ
る。
ちなみに、本発明は本出願人が特願平1−
256382号の出願において提案したピツチコントロ
ール剤に対しても改良関係を有するもので、この
先行発明に比較して2次凝集物の平均粒子径を大
きくしているため、ピツチ除去率は僅かに下がる
もののほぼ同程度に保ちながら紙への定着率が向
上し、他方、紙の中に抄き込まれたときに不透明
度をも向上させるという効果を発揮する。
〔実施例〕
次に実施例により本発明を更に詳細に説明す
る。
実施例、比較例の試験方法は下記の通り。
コロイダルピツチ数
目盛り50μmのヘマストメーターに大きさ22mm
×30mmのカバーグラスをかぶせ、一端より毛細管
によつてこの白水を流し込み、顕微鏡を使用し、
800倍の倍率でコロイダルピツチ数をカウントし
た。このカウント数をカウントした升目数で割
り、升目当りの平均コロイダルピツチ数を得、以
下の式より1cm3当りのコロイダルピツチ数(P)
を算出した。
P=PC×d/V
PC:升目当りの平均コロイダルピツチ数
d:深さの補正係数=1.1
V:升目上の液体の容積
升目上の液体の容積は、深さ0.1mm、底面積
2500μm2であるから、cm3に換算して
P=1.1×PC/2.5×10-7=PC×4.4×106
ピツチ面積
JIS P8208によりピツチ面積を測定
実施例 1
ピツチコントロール剤の調製
吸油量75ml/100g、比表面積100cm2/gの活性
白土を4.5Kg秤取し、25.5Kgの水を加えて濃度15
重量%スラリーを得た。このスラリーに室温撹拌
下で塩化アルミニウム水溶液(Al2O3含有量10
%)、1.44Kg(固形分として)添加し、1時間撹
拌反応させた後、送風乾燥機で温度130℃、4時
間乾燥及び熱処理し放冷した。この反応物を粉砕
し、反応2次凝集物(A)を得た。この反応2次凝集
物(A)の吸油量は110ml/100g、BET法による比表
面積は170m2/g、平均粒径は2.7μmであつた。
次に平均粒径4μmのタルク(吸油量43ml/
100g、比表面積16m2/g)を用意した。
本発明のピツチコントロール剤は、反応2次凝
集物とタルクを第1表に示すように所定の比率で
混合したものである。
図面に示すパルプ漂白工程前の未晒クラフトパ
ルプ(国内針葉樹70%、熱帯広葉樹30%配合)を
洗浄機による洗浄、スクリーンによる除塵、精
選、脱水機による脱水を行う工程において、脱水
機から排出された濃度0.02%の白水ビツトに、
本発明の反応2次凝集物(A)とタルクの混合物をパ
ルプt当り、第1表に示す量を添加した白水を、
スクリーン、脱水機におけるパルプ原料の稀釈に
使用した後の脱水機の出口のパルプのコロイダ
ルピツチ数を測定した。
実施例 2
実施例1において、の反応2次凝集物(A)の代り
に、反応2次凝集物の粉砕時間を短くして、平均
粒径3.2μmとし、吸油量80ml/g、比表面積130
ml/gとした反応2次凝集物(B)を用いる以外は実
施例1と全く同様にして行つた。
比較例 1
実施例1において、反応2次凝集物(A)とタルク
の混合物の代りに、タルクを表に示す量を添加し
た以外は、実施例1と全く同様にして行つた。
比較例 2
実施例1において、反応2次凝集物(A)とタルク
の混合物を添加しない以外は実施例1と全く同様
にして行つた。
参考例 1
実施例1において、反応2次凝集物(A)とタルク
の混合物の代りに、反応2次凝集物(A)のみを添加
する以外は、実施例1と全く同様にして行つた。
参考例 2
実施例2において、反応2次凝集物(B)とタルク
の混合物の代りに、反応2次凝集物(B)のみを添加
する以外は、実施例2と全く同様にして行つた。
実施例1、2、比較例1、2、参考例1、2の
試験結果を第1表に示す。
[Industrial Field of Application] The present invention relates to a pitch control agent. [Prior Art] Countermeasures against pitch troubles in pulp and paper manufacturing processes have been an important issue for a long time. Pitch is a substance that is inevitably mixed in in paper mills, and is mainly used in wood chips, waste paper pulp,
Other than those brought in from rosin sizing agents, etc. and removed from the system along with waste water, and those that are further incorporated into paper, they are accumulated in each process of cooking, beating, and paper making, and are circulated within the system. ing. Furthermore, the pulp processing equipment of each process, the walls of the pulp slurry storage chest, the wires on the paper machine,
Aggregated pitch particles adhere to press rolls, dryer rolls, blankets, canvases, etc., causing various problems. Conventional countermeasures include, for example, strengthening the seasoning of the raw material wood, strengthening the cleaning of the raw material pulp, selecting raw materials with less pitch, suppressing foaming of raw materials: white water, surfactants, water-soluble polymer dispersants, Methods include adding protective colloids such as starch and gelatin, ethylenediaminetetraacetic acid (EDTA), and talc to the mixer. In addition to the above, it is conventionally known to use diatomaceous earth, silica, clay, bentonite, acid clay, talc, etc. as pitch removers by adding them to pulp raw materials or white water systems. None of the pitch removers mentioned above is a decisive factor in pitch control, and in response to the increase in pitch due to the deterioration of raw material quality in recent years, various methods such as pulp and waste paper pulp manufacturing processes, paper manufacturing processes, white water treatment processes, etc. It has not yet become an effective pitch control agent capable of adsorbing even ionic pitch in certain locations. The present inventors previously proposed a new pitch control agent and pitch control method in JP-A-1-104892. This pitch control agent is a secondary aggregate of reaction between acid-treated acid clay and aluminum salt, and has physical properties such as an oil absorption of 70 ml/100 g or more and a specific surface area of 130 m 2 /g or more. . This pitch control agent is made of acid-treated acid clay treated with aluminum salt, so it strengthens the attraction of charged pitch particles in water and uses a large specific surface area to enhance the pitch control effect. However, this pitch control agent is not effective against all pitches present in the pulp and paper manufacturing processes, and its effectiveness reaches a plateau even if it is added beyond a certain level.For example, when added to white water, the pitch removal rate is generally low. It is difficult to increase the ratio to about 50% or more. [Problem to be solved by the invention] In light of the above-mentioned current situation, in a situation where the quality of raw materials is decreasing, the amount of used paper is increasing, and the amount of waste paper is increasing, it is difficult to use it in any place such as pulp manufacturing process or finger manufacturing process. There has been a need for a pitch control agent that is effective against various pitches even when the pitch is removed, and has a higher pitch removal rate than conventional pitch control agents. [Means for Solving the Problems] The present invention provides a secondary reaction aggregate of an acid-treated acid clay and an aluminum salt, and has an oil absorption of 80%.
ml/100g or more, a specific surface area of 130m 2 /g or more, and an average particle size of 2.7μ or more and talc with an average particle size of 5μm or less in a weight ratio of 1:3.
This pitch control agent is characterized by being mixed at a ratio of 3:1 to 3:1. Although it is not clear why the pitch control agent of the present invention is so effective, the following reasons may be considered. That is, there are several types of pitches, and they also differ in size, and it is thought that depending on the type of pitch control agent, there is selectivity in adsorption to pitches. It is thought that there is a difference in the type of pitch adsorbed between the secondary aggregates of the reaction between acid-treated acid clay and aluminum salt and talc. Therefore, when the pitch control agent of the present invention is used, each pitch control agent shares adsorption of pitches having different properties, and it is considered that more pitches are controlled. The pitch control agent of the present invention is a mixture of reaction secondary aggregates and talc, but the mixing ratio may be such that the reaction secondary aggregates cannot be used alone even if the reaction secondary aggregates are too much or too little. In comparison, no significant pitch effect is obtained, and the mixing ratio of talc in the reaction secondary agglomerates is required to be from 3:1 to 1:3 by weight. According to experiments conducted by the present inventors, it has been confirmed that the highest pitch removal rate can be obtained when the mixing ratio is 1:1. Since the pitch control agent of the present invention efficiently adsorbs and removes pitches having various properties as described above, it can be effectively used in all parts of the pulp manufacturing process and paper manufacturing process. When it is added to the stock in the pulp manufacturing process or paper manufacturing process, a preferable pitch removal effect can be obtained by using it in an amount of 0.5 to 3% by weight based on the pulp (solid content). On the other hand, as the present applicant has already proposed in JP-A-1-104892, pitch control agents are more likely to accumulate pitch through circulation than when added to pulp or stock in the papermaking process, which has relatively little pitch. Adding it to the white water that circulates through the pulp manufacturing process, used paper pulp manufacturing process, and paper manufacturing process allows for the removal of various pitches with different properties in a small amount and efficiently. Examples of where to add the pitch control agent to white water in each process and how to use the white water include adding the pitch control agent of the present invention to high-concentration white water obtained from paper stock recovery equipment for white water in the papermaking process, and adding the pitch control agent of the present invention to beaten pulp. The pitch control agent of the present invention is added to the recycled white water of the pulp manufacturing process and the recycled white water of waste paper in the waste paper processing process. In addition, the pitch control agent of the present invention is added to the dilution prior to flotation in the waste paper deinking process, and the white water generated in the final deinking process is used. The pitch control method using the pitch control agent of the present invention can achieve remarkable effects in controlling pitch spots on paper and pitch trouble in each process by performing these methods in parallel at two or more locations. The amount of the mixture of the acid-treated acid clay (activated clay) and the aluminum salt, which is the pitch control agent of the present invention, and the mixture of talc and the white water in each of the above steps is determined by the white water solid content (pulp ), a sufficient effect is exhibited at 0.1 to 3% by weight. In reality, the amount added varies depending on the process, for example, 0.1 to 0.5% by weight in the pulp process and 0.2% in the waste paper processing process.
A preferable removal effect is obtained at ~1% by weight. In addition, when the pitch control agent of the present invention is applied to white water, it is added in an amount of 0.1 to 3% by weight based on the paper stock content in the white water, so the amount used is as follows: 0.014~ for the fiber content of pulp or paper stock when used as 15%
The amount is 0.45% by weight, and the pitch control effect can be achieved with about 1/10 of the amount of pitch control agent added to ordinary pulp raw materials. By the way, the present invention was filed by the applicant in patent application No.
This is also an improvement over the pitch control agent proposed in the application No. 256382, and the average particle size of the secondary aggregates is increased compared to this prior invention, so the pitch removal rate is slightly lower. It has the effect of improving the fixation rate on paper while keeping it at about the same level, and also improving the opacity when it is incorporated into paper. [Example] Next, the present invention will be explained in more detail with reference to Examples. The test methods for Examples and Comparative Examples are as follows. Colloidal pitch number Hemastometer with scale of 50μm and size 22mm
Cover with a 30 mm cover glass, pour this white water through a capillary tube from one end, and use a microscope.
The number of colloidal pits was counted at 800x magnification. Divide this count number by the number of squares counted to obtain the average number of colloidal pitches per square, and use the following formula to calculate the number of colloidal pitches per cm3 (P).
was calculated. P=PC×d/V PC: Average number of colloidal pits per square d: Depth correction coefficient = 1.1 V: Volume of liquid above the square The volume of liquid above the square is 0.1 mm in depth and base area.
Since it is 2500 μm 2 , converted to cm 3 P = 1.1 × PC / 2.5 × 10 -7 = PC × 4.4 × 10 6 pitch area Measure pitch area according to JIS P8208 Example 1 Preparation of pitch control agent Oil absorption 75 ml /100g, specific surface area 100cm 2 /g 4.5Kg of activated clay was weighed out, and 25.5Kg of water was added to make the concentration 15.
A weight percent slurry was obtained. An aqueous aluminum chloride solution (Al 2 O 3 content 10
%), 1.44 kg (as solid content) was added, stirred and reacted for 1 hour, then dried and heat treated in a blow dryer at a temperature of 130° C. for 4 hours, and allowed to cool. This reaction product was pulverized to obtain a secondary reaction aggregate (A). The oil absorption amount of this reaction secondary aggregate (A) was 110 ml/100 g, the specific surface area by BET method was 170 m 2 /g, and the average particle size was 2.7 μm. Next, talc with an average particle size of 4 μm (oil absorption 43 ml/
(100 g, specific surface area 16 m 2 /g) was prepared. The pitch control agent of the present invention is a mixture of a reaction secondary aggregate and talc in a predetermined ratio as shown in Table 1. The unbleached kraft pulp (contains 70% domestic softwood and 30% tropical hardwood) before the pulp bleaching process shown in the drawing is washed with a washing machine, dust removed with a screen, sorted, and dehydrated with a dehydrator. In the white water bit with a concentration of 0.02%,
White water to which the mixture of the reaction secondary aggregate (A) of the present invention and talc is added in the amount shown in Table 1 per ton of pulp,
The number of colloidal pitches of the pulp at the outlet of the dehydrator after being used to dilute the pulp raw material in the screen and dehydrator was measured. Example 2 In Example 1, instead of the reaction secondary aggregate (A), the reaction secondary aggregate was crushed for a shorter time to have an average particle size of 3.2 μm, an oil absorption of 80 ml/g, and a specific surface area of 130
The reaction was carried out in exactly the same manner as in Example 1 except that the reaction secondary aggregate (B) was used at ml/g. Comparative Example 1 The same procedure as in Example 1 was conducted except that talc was added in the amount shown in the table instead of the mixture of the secondary reaction aggregate (A) and talc. Comparative Example 2 The same procedure as in Example 1 was carried out except that the mixture of the secondary reaction aggregate (A) and talc was not added. Reference Example 1 Example 1 was carried out in exactly the same manner as in Example 1, except that only the reaction secondary aggregate (A) was added instead of the mixture of the reaction secondary aggregate (A) and talc. Reference Example 2 Example 2 was carried out in exactly the same manner as in Example 2, except that only the reaction secondary aggregate (B) was added instead of the mixture of the reaction secondary aggregate (B) and talc. The test results of Examples 1 and 2, Comparative Examples 1 and 2, and Reference Examples 1 and 2 are shown in Table 1.
【表】
第1表の結果によれば、本発明のピツチコント
ロール剤は、反応2次凝集物(A)とタルクの混合比
率3:1(実施例1−2)〜1:3(実施例1−
3)の範囲では、反応2次凝集物(A)を単独使用し
た場合(参考例1)よりピツチ除去効果が向上し
ている。殊に反応2次凝集物(A)とタルクの混合比
率1:1ののとき(実施例1−1)に最もピツチ
除去率が高くなつている。
また、実施例2の反応2次凝集物(B)(吸油量80
ml/g)をタルクと1:1で使用した場合は、実
施例1−1よりピツチ除去率は下がるが、反応2
次凝集物(B)単独使用(参考例2)よりピツチ除去
率は遥かに向上する。
実施例 3、4
実施例1で得られた反応2次凝集物(A)とタルク
の1:1の混合物である本発明のピツチコントロ
ール剤を準備した。
次いで熱帯広葉樹化学パルプ、針葉樹化学パル
プ、針葉樹機械パルプ、脱墨古紙パルプを重量で
25対15対40対20の割合で混合し、更にロジンサイ
ズ剤5Kg/パルプt、硫酸バンド20Kg/パルプt
を添加混合し、濃度3重量%のパルプスラリーを
調成した。このパルプスラリーに、前記反応2次
凝集物(A)とタルクの1:1の混合物をパルプ固形
分に対し、1重量%(実施例3)及び0.5重量%
(実施例4)添加し、5分間撹拌した。このピツ
チコントロール剤添加によるピツチ除去効果を下
記の試験法により評価した。結果は第2表に示
す。
比較例 3
実施例3において、本発明の反応2次凝集物の
代りにタルク(吸油量40ml/100g、比表面積10
m2/g)を用いる以外は実施例3と全く同様にし
てピツチ面積を測定した。
比較例 4
実施例3において、本発明の反応2次凝集物の
代りに市販タルク系ピツチコントロール剤A(以
下市販品Aと略記)(吸油量47ml/100g、比表面
積16m2/g)を用いる以外は、実施例3と全く同
様にしてピツチ面積を測定した。
比較例 5
実施例3において、本発明の反応2次凝集物の
代りに、活性白土(吸油量80ml/100g、比表面
積110m2/g)を用いる以外は実施例3と全く同
様にしてピツチ面積を測定した。
比較例 6
実施例3において、本発明の反応2次凝集物を
パルプ固形分に対し、0.3%添加する以外は、実
施例3と全く同様にしてピツチ面積を測定した。
比較例 7
実施例3において、本発明の反応2次凝集物を
添加しない以外は、実施例3と全く同様にしてピ
ツチ面積を測定した。
実施例3、4、比較例3〜7の試験結果を第2
表に示す。[Table] According to the results in Table 1, the pitch control agent of the present invention has a mixing ratio of reaction secondary aggregate (A) and talc of 3:1 (Example 1-2) to 1:3 (Example 1-2). 1-
In the range of 3), the pitch removal effect is improved compared to the case where the reaction secondary aggregate (A) is used alone (Reference Example 1). In particular, the pitch removal rate was highest when the mixing ratio of the reaction secondary aggregate (A) and talc was 1:1 (Example 1-1). In addition, the reaction secondary aggregate (B) of Example 2 (oil absorption 80
ml/g) with talc at a ratio of 1:1, the pitch removal rate is lower than in Example 1-1, but the reaction 2
The pitch removal rate is much improved compared to using the secondary aggregate (B) alone (Reference Example 2). Examples 3 and 4 A pitch control agent of the present invention, which is a 1:1 mixture of the reaction secondary aggregate (A) obtained in Example 1 and talc, was prepared. Next, tropical hardwood chemical pulp, softwood chemical pulp, softwood mechanical pulp, and deinked waste paper pulp are classified by weight.
Mix in a ratio of 25:15:40:20, and then add 5 kg of rosin sizing agent/t of pulp and 20 kg of sulfuric acid/t of pulp.
were added and mixed to prepare a pulp slurry having a concentration of 3% by weight. To this pulp slurry, a 1:1 mixture of the reaction secondary aggregate (A) and talc was added at 1% by weight (Example 3) and 0.5% by weight based on the pulp solid content.
(Example 4) Added and stirred for 5 minutes. The effect of removing pitch by adding this pitch control agent was evaluated by the following test method. The results are shown in Table 2. Comparative Example 3 In Example 3, talc (oil absorption 40 ml/100 g, specific surface area 10
The pitch area was measured in the same manner as in Example 3, except that the pitch area was measured using the following formula: (m 2 /g). Comparative Example 4 In Example 3, commercially available talc-based pitch control agent A (hereinafter abbreviated as commercial product A) (oil absorption 47 ml/100 g, specific surface area 16 m 2 /g) was used instead of the reaction secondary aggregate of the present invention. Except for this, the pitch area was measured in the same manner as in Example 3. Comparative Example 5 In Example 3, pitch area was determined in exactly the same manner as in Example 3, except that activated clay (oil absorption 80 ml/100 g, specific surface area 110 m 2 /g) was used instead of the reaction secondary aggregate of the present invention. was measured. Comparative Example 6 In Example 3, the pitch area was measured in exactly the same manner as in Example 3, except that 0.3% of the reaction secondary aggregate of the present invention was added to the pulp solid content. Comparative Example 7 In Example 3, the pitch area was measured in exactly the same manner as in Example 3, except that the reaction secondary aggregate of the present invention was not added. The test results of Examples 3 and 4 and Comparative Examples 3 to 7 are
Shown in the table.
以上詳述したように本発明のピツチコントロー
ル剤は、ピツチの多い熱帯広葉樹の使用或いは古
紙パルプ使用の増大等近年の原料品質の悪化に伴
うピツチ増に対応して発明されたものである。
本発明のピツチコントロール剤は、酸性白土の
酸処理物とアルミニウム塩の反応2次凝集物、特
に吸油量と比表面積が大きい反応2次凝集物とタ
ルクの混合物から成り、従来のピツチコントロー
ル剤より格段にすぐれたピツチ吸着性能を有する
ものである。
本発明のピツチコントロール剤は、通常のパル
プ又は紙料に添加してピツチ除去効果に著効があ
るほか、パルプ、脱墨古紙パルプの製造工程、製
紙工程の白水処理において循環再使用される白水
に添加することにより、パルプに起因する白水の
循環中に増加した酸性白土中の性質の異なるピツ
チを反応2次凝集物とタルクがそれぞれ分担吸着
して相乗効果を発揮し、パルプ、古紙パルプの製
造工程、製紙工程中のピツチ濃度を大幅に低下さ
せ、結果的に得られるパルプ、紙のピツチを従来
のピツチコントロール剤を用いた場合より大幅に
除去して品質を向上することができる。
従つて、本発明はパルプ、製紙工場におけるピ
ツチトラブルを大幅に減少させることができる従
来にないすぐれたピツチコントロール剤である。
As detailed above, the pitch control agent of the present invention was invented in response to the increase in pitch caused by the deterioration of raw material quality in recent years, such as the increase in the use of tropical hardwoods that have a lot of pitch or the increase in the use of waste paper pulp. The pitch control agent of the present invention is composed of a reaction secondary aggregate of an acid-treated acid clay and an aluminum salt, especially a mixture of a reaction secondary aggregate with a large oil absorption and specific surface area, and talc, and is better than conventional pitch control agents. It has extremely excellent pitch adsorption performance. The pitch control agent of the present invention is effective in removing pitch when added to ordinary pulp or paper stock, and can also be used to circulate and reuse white water in the manufacturing process of pulp, deinked waste paper pulp, and white water treatment in the paper manufacturing process. By adding this to talc, the reaction secondary aggregates and talc each absorb pitches of different properties in the acid clay that increase during the circulation of white water caused by pulp, and exhibit a synergistic effect, resulting in a synergistic effect. The pitch concentration during the manufacturing process and papermaking process can be significantly reduced, and the quality of the resulting pulp and paper can be improved by removing pitch to a greater extent than when using conventional pitch control agents. Therefore, the present invention is an unprecedented pitch control agent that can significantly reduce pitch troubles in pulp and paper mills.
図面はパルプ製造工程(晒クラフトパルプ)の
フローを示す略図である。
The drawing is a schematic diagram showing the flow of the pulp manufacturing process (bleached kraft pulp).
Claims (1)
応2次凝集物であつて、かつ吸油量が80ml/
100g以上、比表面積が130m2/g以上で、更に平
均粒子径が2.7μ以上の前記反応2次凝集物と平均
粒径5μm以下のタルクとを重量比で1:3ないし
3:1の割合で混合してなることを特徴とするピ
ツチコントロール剤。1 A secondary reaction aggregate of acid-treated acid clay and aluminum salt, and has an oil absorption of 80ml/
A weight ratio of 1:3 to 3:1 of the reaction secondary aggregate having a specific surface area of 100 g or more, a specific surface area of 130 m 2 /g or more, and an average particle size of 2.7 μm or more and talc having an average particle size of 5 μm or less. A pitch control agent characterized by being mixed with.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24633589A JPH03113092A (en) | 1989-09-25 | 1989-09-25 | Pitch-controlling agent |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP24633589A JPH03113092A (en) | 1989-09-25 | 1989-09-25 | Pitch-controlling agent |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03113092A JPH03113092A (en) | 1991-05-14 |
| JPH0541750B2 true JPH0541750B2 (en) | 1993-06-24 |
Family
ID=17147035
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP24633589A Granted JPH03113092A (en) | 1989-09-25 | 1989-09-25 | Pitch-controlling agent |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03113092A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2709765B1 (en) * | 1993-09-10 | 1995-11-24 | Luzenac Talc | Process for treating paper pulp and enzymatic aqueous preparation for its implementation. |
-
1989
- 1989-09-25 JP JP24633589A patent/JPH03113092A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03113092A (en) | 1991-05-14 |
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