JPS6228239B2 - - Google Patents

Info

Publication number
JPS6228239B2
JPS6228239B2 JP5347977A JP5347977A JPS6228239B2 JP S6228239 B2 JPS6228239 B2 JP S6228239B2 JP 5347977 A JP5347977 A JP 5347977A JP 5347977 A JP5347977 A JP 5347977A JP S6228239 B2 JPS6228239 B2 JP S6228239B2
Authority
JP
Japan
Prior art keywords
mol
vinyl acetate
saponification
aqueous solution
units
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
Application number
JP5347977A
Other languages
Japanese (ja)
Other versions
JPS53139811A (en
Inventor
Takeshi Matsuyama
Shuji Tsutsumi
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.)
Nippon Synthetic Chemical Industry Co Ltd
Original Assignee
Nippon Synthetic Chemical Industry Co Ltd
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 Nippon Synthetic Chemical Industry Co Ltd filed Critical Nippon Synthetic Chemical Industry Co Ltd
Priority to JP5347977A priority Critical patent/JPS53139811A/en
Publication of JPS53139811A publication Critical patent/JPS53139811A/en
Publication of JPS6228239B2 publication Critical patent/JPS6228239B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Paper (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明はオフセツト輪転印刷用原紙として好適
なサイズ紙を提供することを目的とする。 紙の表面サイズ剤として従来酸化デンプン、ア
ルギン酸ソーダ、カルボキシメチルセルロース、
ポリアクリルアミド、ポリビニルアルコールなど
がそれぞれ単独で或いは2種以上を混合して使用
されているが、オフセツト輪転印刷の普及に伴な
いいくつかのトラブルが生じている。その最も大
きいものはブリスター抵抗の不足である。即ち上
記表面サイズを施した原紙に透気性を有するコー
ト層を設けたコートに連続的にオフセツト輪転印
刷を行なつた後直ちに直火加熱(約350℃)によ
り乾燥を行なう場合、紙層中の水分に起因する水
蒸気及び空気が表面に抜けずに内部にたまつて火
ぶくれ現象を起すのである。従つてオフセツト輪
転印刷においては直火加熱に対し紙層が火ぶくれ
を起さないように、(イ)紙のZ軸強度(紙面に対し
垂直方向の強度)が大きく、かつ(ロ)水蒸気・空気
の透過性が大きいこと、の2点が特り要求される
のであるが、従来の表面サイズ剤によつてはこれ
らの要求には充分に対応しえない状態であつた。 本発明はこのような従来のオフセツト輪転印刷
用原紙の問題を「マレイン酸エステル―酢酸ビニ
ル共重合体ケン化物を更にアルカリ水溶液の存在
下で二次ケン化して得られるマレイン酸ジアルカ
リ塩単位0.5〜20モル%、酢酸ビニル単位のケン
化度97モル%以上のケン化物」の水溶液をサイジ
ング液として用いることによつて解決したもので
ある。 上記特定の高度ケン化物の水溶液をサイジング
液として用いることにより、汎用の酸化デンプン
使用の場合に比しZ軸強度は約4〜8割も増大
し、ポリビニルアルコールに比しても約〜3割増
大する。透気性の比較では本発明のサイズ処理紙
も酸化デンプンサイズ処理紙も共に良い結果を与
え、一方ポリビニルアルコールサイズ処理紙はこ
れらに比べると透気性は劣る。総合的に示せば次
のようになる。 Z軸強度 透気性 本発明のケン化物 ○ ○ 酸化デンプン × ○ ポリビニルアルコール △ △ 本発明で使用されるケン化物は、マレイン酸モ
ノメチル、マレイン酸モノエチル、マレイン酸モ
ノプロピル、マレイン酸モノブチル等のマレイン
酸モノエステル、マレイン酸ジメチル、マレイン
酸ジエチル、マレイン酸ジプロピル、マレイン酸
ジブチル等のマレイン酸ジエステルを代表例とす
るマレイン酸エステルと酢酸ビニルとの共重合体
を苛酷なアルカリケン化条件下にケン化すること
によつてはじめて製造される。即ちメタノールな
どの溶媒中で苛性アルカリやアルカリ金属アルコ
ラート触媒存在下に常法より上記共重合体をケン
化するだけでは共重合体中のマレイン酸単位はジ
アルカリ塩型にはらず、又酢酸ビニル単位のケン
化度もせいぜい95〜96%程度にまで上がるにすぎ
ず、それ以上のケン化は非常に困難である。これ
はマレイン酸単位の両隣りの酢酸ビニル単位のケ
ン化が容易に進行しないためと考えられる。従つ
て上式にようにマレイン酸単位をジアルカリ塩に
しかつ酢酸ビニル単位のケン化度を97モル%以上
にするためには、前記常法により得れた部分ケン
化物をさらにアルカリ水溶液、例えば苛性ソーダ
水溶液、苛性カリ水溶液中に投入するか上記部分
ケン化物にアルカリ水溶液触媒を付着させて加熱
し、ケン化反応をさらに進めなければならない。 未だジアルカリ塩単位に変換せずマレイン酸エ
ステルとして多量に残在している場合は透気性が
小さく、直火加熱に際し火ぶくれを起す危険があ
る。又ジアルカリ塩単位となつていてもそのモル
分率が0.5モル%未満の場合はZ軸強度が劣り、
一方20モル%を越えるときは重合度が低下するた
めに強度が不足する。 酢酸ビニル単位のモル分率mとビニルアルコー
ル単位のモル分率nとの和は残りの80〜99.5モル
%となるが、100n/m+nは97〜100、即ち酢酸ビ
ニル単 位のケン化度は97モル%以上でなければならず、
酢酸ビニル単位のケン化度が97モル%未満の場合
は透気性が劣り、火ぶくれの原因となる。特に好
ましい結果は酢酸ビニル単位のケン化度が98モル
%以上の場合に得られる。 本発明サイズ剤を用いてオフセツト輪転印刷用
原紙をサイズするにあたつては該サイズ剤をの方
法を実施するにあたつては上記ケン水に溶解して
固形分約0.5〜10%程度、20℃における4%水溶
液の粘度を5〜100cps程度に調節し、サイズプ
レスコート、カレンダースタツクコート、ロール
コートなどにより紙の表面に塗布した後乾燥する
という従来公知の表面サイズ方法がいずれも採用
しうる。なお上記ケン化物は単独で用いるほか、
酸化デンプン、ポリビニルアルコールなど従来公
知の表面サイズ剤や少量の硫酸バン土などと併用
しても差支えない。特に酸化デンプンとの併用は
経済上、品質上有用である。又本発明の方法を適
用する原紙は若干のアルミナ分(硫酸バン土な
ど)を含有していることがその効果を充分発揮せ
しめる上で好ましい。 次に実施例をあげて本発明をさらに説明する。
以下「部」、「%」とあるのは特にことわりのない
限り重量基準で表わしたものである。 実施例 1 マレイン酸モノメチル含量3.0モル%のマレイ
ン酸モノメチル―酢酸ビニル共重合体をメタノー
ル中苛性ソーダ触媒の存在下にケン化して酢酸ビ
ニル単位のケン化度95.0モル%のマレイン酸モノ
メチル―酢酸ビニル―ビニルアルコール共重合体
粒子を得、次にこの粒子を苛性ソーダの5%水溶
液中に投入して温度85℃で2時間加熱撹拌した。
かくして得られた生成物はマレイン酸ジナトリウ
ム単位3.0モル%を有し、酢酸ビニル単位のケン
化度は99.5モル%であつた。 次にかくして得られたケン化物の3%水溶液を
調製し(20℃における粘度18.5cps)、若干の硫酸
バン土を含む坪量60g/m2の上質紙にサイズプレ
スコーターを用いて固形分が1.0g/m2になるよ
うに塗布、乾燥した後、温度80〜85℃のスーパー
カレンダーを1回通して表面サイズした。このサ
イズ紙を温度20℃、関係湿度65%の条件下に72時
間放置してからZ軸強度、透気度、吸油度、IGT
ピツク強度及びステキヒトサイズ度を測定した。
又このサイズ紙の表裏にコート層を設けた後連続
的にオフセツト輪転印刷を行ない、ついで直火加
熱(約350℃)により乾燥を行なつたときの火ぶ
くれの発生の有無を見た。結果を第1表に示す。 対照例 1 酸化デンプンの6%水溶液を用いたほかは実施
例1と同様にしてサイズプレスを行なつた。(3
%水溶液は性質が劣るので6%水溶液とした。) 対照例 2 重合度1700、ケン化度99.5モル%のポリビニル
アルコールの3%水溶液を用いたほかは実施例1
と同様にしてサイズプレスを行なつた。 対照例 3 重合度500、ケン化度88.0モル%のポリビニル
アルコールの3%水溶液を用いたほかは実施例1
と同様にしてサイズプレスを行なつた。 対照例1〜3の結果を第1表に合せて示す。
An object of the present invention is to provide paper of a suitable size as a base paper for offset rotary printing. Conventional paper surface sizing agents include oxidized starch, sodium alginate, carboxymethyl cellulose,
Polyacrylamide, polyvinyl alcohol, and the like are used alone or in combination of two or more, but as offset rotary printing becomes more widespread, several problems have arisen. The biggest one is the lack of blister resistance. In other words, if a coat of base paper with the above surface size and an air-permeable coating layer is subjected to continuous offset rotary printing and then immediately dried by direct heating (approximately 350°C), the Water vapor and air caused by moisture do not escape to the surface and accumulate inside, causing blistering. Therefore, in offset rotary printing, in order to prevent the paper layer from blistering when heated by direct flame, it is necessary to (a) have high Z-axis strength (strength in the direction perpendicular to the paper surface) of the paper, and (b) resist water vapor. - High air permeability is particularly required, but conventional surface sizing agents have not been able to sufficiently meet these requirements. The present invention solves the problem of conventional offset rotary printing base paper by "dialkali maleic acid salt unit 0.5 to This problem was solved by using as a sizing liquid an aqueous solution of a saponified product with a degree of saponification of vinyl acetate units of 20 mol % or more and 97 mol % or more. By using an aqueous solution of the above-mentioned highly saponified product as a sizing liquid, the Z-axis strength increases by about 40 to 80% compared to using general-purpose oxidized starch, and about 30% more than polyvinyl alcohol. make it big In a comparison of air permeability, both the sized paper of the present invention and the oxidized starch sized paper give good results, while the polyvinyl alcohol sized paper has inferior air permeability. The overall result is as follows. Z-axis strength Air permeability Saponified products of the present invention ○ ○ Oxidized starch × ○ Polyvinyl alcohol △ △ The saponified products used in the present invention include maleic acids such as monomethyl maleate, monoethyl maleate, monopropyl maleate, and monobutyl maleate. Copolymers of maleic acid esters and vinyl acetate, representative examples of which are monoesters, maleic diesters such as dimethyl maleate, diethyl maleate, dipropyl maleate, and dibutyl maleate, are saponified under severe alkaline saponification conditions. It is manufactured for the first time by doing so. That is, if the above copolymer is simply saponified by a conventional method in the presence of a caustic alkali or alkali metal alcoholate catalyst in a solvent such as methanol, the maleic acid units in the copolymer will not convert to the dialkali salt type, and the vinyl acetate units will not change to the dialkali salt type. The degree of saponification increases to only about 95 to 96% at most, and saponification beyond that level is extremely difficult. This is thought to be because saponification of the vinyl acetate units on both sides of the maleic acid unit does not proceed easily. Therefore, in order to convert the maleic acid unit into a dialkali salt and to make the degree of saponification of the vinyl acetate unit 97 mol% or more as shown in the above formula, the partially saponified product obtained by the above conventional method is further mixed with an alkaline aqueous solution, such as caustic soda. It is necessary to further advance the saponification reaction by adding the partially saponified product into an aqueous solution or aqueous caustic potassium solution, or by attaching an alkaline aqueous catalyst to the partially saponified product and heating it. If a large amount of maleic acid ester remains without being converted into dialkali salt units, the gas permeability is low and there is a risk of blistering when heated over an open flame. Furthermore, even if dialkali salt units are present, if the molar fraction is less than 0.5 mol%, the Z-axis strength will be poor;
On the other hand, when it exceeds 20 mol%, the degree of polymerization decreases, resulting in insufficient strength. The sum of the mole fraction m of vinyl acetate units and the mole fraction n of vinyl alcohol units is the remaining 80 to 99.5 mol%, but 100n/m+n is 97 to 100, that is, the degree of saponification of vinyl acetate units is 97. Must be greater than or equal to mol%,
If the degree of saponification of vinyl acetate units is less than 97 mol%, air permeability will be poor and cause blisters. Particularly favorable results are obtained when the degree of saponification of vinyl acetate units is 98 mol % or more. When sizing base paper for offset rotary printing using the sizing agent of the present invention, the sizing agent should be dissolved in the above-mentioned saline water to have a solid content of about 0.5 to 10%. All conventional surface sizing methods are adopted, in which the viscosity of a 4% aqueous solution at 20°C is adjusted to about 5 to 100 cps, and the solution is coated on the paper surface by size press coating, calendar stack coating, roll coating, etc., and then dried. I can do it. In addition to using the above saponified products alone,
It may be used in combination with conventionally known surface sizing agents such as oxidized starch and polyvinyl alcohol, as well as a small amount of sulfuric acid. In particular, the combination with oxidized starch is economically and qualitatively useful. Further, it is preferable that the base paper to which the method of the present invention is applied contains a small amount of alumina (aluminium sulfate, etc.) in order to fully exhibit its effects. Next, the present invention will be further explained with reference to Examples.
Hereinafter, "parts" and "%" are expressed on a weight basis unless otherwise specified. Example 1 A monomethyl maleate-vinyl acetate copolymer with a monomethyl maleate content of 3.0 mol% was saponified in methanol in the presence of a caustic soda catalyst to obtain a monomethyl maleate-vinyl acetate copolymer with a degree of saponification of vinyl acetate units of 95.0 mol%. Vinyl alcohol copolymer particles were obtained, and then the particles were poured into a 5% aqueous solution of caustic soda and heated and stirred at a temperature of 85° C. for 2 hours.
The product thus obtained contained 3.0 mol% of disodium maleate units, and the degree of saponification of vinyl acetate units was 99.5 mol%. Next, a 3% aqueous solution of the saponified product thus obtained was prepared (viscosity 18.5 cps at 20°C), and the solid content was coated on high-quality paper with a basis weight of 60 g/m 2 containing some sodium sulfate using a size press coater. After coating and drying to a concentration of 1.0 g/m 2 , the surface was sized by passing it once through a super calender at a temperature of 80 to 85°C. This size paper was left for 72 hours at a temperature of 20℃ and relative humidity of 65%, and then Z-axis strength, air permeability, oil absorption, and IGT were measured.
Pick strength and Steckigt sizing were measured.
In addition, after coating layers were provided on the front and back sides of this size paper, continuous offset rotary printing was performed, and then drying was performed by direct heating (approximately 350°C) to see whether or not blistering occurred. The results are shown in Table 1. Control Example 1 Size press was carried out in the same manner as in Example 1 except that a 6% aqueous solution of oxidized starch was used. (3
% aqueous solution has inferior properties, so a 6% aqueous solution was used. ) Control Example 2 Example 1 except that a 3% aqueous solution of polyvinyl alcohol with a degree of polymerization of 1700 and a degree of saponification of 99.5 mol% was used.
Size press was performed in the same manner as above. Control example 3 Example 1 except that a 3% aqueous solution of polyvinyl alcohol with a degree of polymerization of 500 and a degree of saponification of 88.0 mol% was used.
Size press was performed in the same manner as above. The results of Control Examples 1 to 3 are also shown in Table 1.

【表】 第1表からも明らかなように、本願発明おいて
はサイズ紙の乾燥にあたりロールとの剥離性が良
好である上、Z軸強度が特に大きく、透気性は大
きいという好ましい結果を示しており、又吸油
度、IGTピツク強度、ステキヒトサイズ度も実用
上何ら支障はない。又本願発明のサイズ紙からコ
ート紙を作り、これをオフセツト輪転印刷に供し
て直火加熱を行なつても火ぶくれ現象は全く生じ
ない。 これに対し酸化デンプンを用いた対照例1では
サイズ紙のZ軸強度が不足するため、オフセツト
輪転印刷時の直火加熱に際し火ぶくれ現象が見ら
れる。 又ポリビニルアルコールの完全ケン化物を用い
た対照例2はN軸強度、透気性共若干劣つている
ため、直火加熱に際しやや火ぶくれを起す。なお
ポリビニルアルコールの部分ケン化物を用いた対
照例3はZ軸強度が劣り、透気性も著しく劣るた
め、火ぶくれ現象が著しい。さらにポリビニルア
ルコールを用いたときは、完全ケン化物であつて
も部分ケン化物であつても、サイズ紙を乾燥する
ときの乾燥ロールとの剥離性が劣るという難点が
ある。 実施例 2 マレイン酸モノメチル含量10.0モル%のマレイ
ン酸モノメチル―酢酸ビニル共重合体を一旦メタ
ノール溶媒中苛性ソーダ触媒存在下にケン化して
酢酸ビニル単位のケン化度90.0モル%のマレイン
酸モノメチル―酢酸ビニル―ビニルアルコール共
重合体粒子を得た後、この粒子に40%苛性ソーダ
水溶液をふりかけ、ついでヘンシエルミキサーで
均一混合することによりマレイン酸ジナトリウム
単位9.0モル%、マレイン酸モノメチル単位1.0モ
ル%、酢酸ビニル単位のケン化度99.5モル%の共
重合体ケン化物を得た。この共重合体ケン化物を
水に加熱溶解して3%水溶液を調整し、実施例1
と同様にしてサイズプレスを行なつた。 対照例 4 実施例1における第1段目のケン化品、即ちマ
レイン酸モノメチル含量3.0モル%、酢酸ビニル
単位のケン化度95.0モル%のマレイン酸モメメチ
ル―酢酸ビニル―ビニルアルコール共重合体の3
%水溶液を用た実施例1と同様にしてサイズプレ
スを行なつた。 実施例 3 マレイン酸モノブチル含量5.0モル%のマレイ
ン酸モノブチル―酢酸ビニル共重合体を最初メタ
ノール中で、次に水中でそれぞれ苛性ソーダ触媒
存在下にケン化してマレイン酸ジナトリウム単位
4.8モル%、マレイン酸モノブチル単位0.2モル
%、酢酸ビニル単位のケン化度99.5モル%の共重
合体ケン化物を得た。この共重合体ケン化物の3
%水溶液を用いて実施例1と同様にしてサイズプ
レスを行なつた。 実施例 4 無水マレイン酸と酢酸ビニルとをメタノール中
で重合させることによりマレイン酸モノメチル含
量3.0モル%のマレイン酸モノメチル―酢酸ビニ
ル共重合体を得た。無水マレイン酸は重合体中で
はマレイン酸モノメチル単位に変換している。次
にこの共重合体を最初メタノール中で、次に水中
で苛性ソーダ触媒によりケン化してマレイン酸ジ
ナトリウム単位3.0モル%、酢酸ビニル単位のケ
ン化度99.7モル%の共重合体を得た。この共重合
体の3%水溶液を用いて実施例1と同様にしてサ
イズプレスを行なつた。 実施例2〜4及び対照例4の結果を第2表に示
す。
[Table] As is clear from Table 1, the present invention shows favorable results such as good releasability from the roll when drying size paper, particularly high Z-axis strength, and high air permeability. In addition, the oil absorption, IGT pick strength, and Steckigt size do not pose any practical problems. Furthermore, even if coated paper is made from the size paper of the present invention, subjected to offset rotary printing, and heated over direct flame, no blistering phenomenon occurs at all. On the other hand, in Comparative Example 1 using oxidized starch, the Z-axis strength of the sized paper was insufficient, so a blistering phenomenon was observed during direct heating during offset rotary printing. Furthermore, Comparative Example 2, which used completely saponified polyvinyl alcohol, was slightly inferior in both N-axis strength and air permeability, and therefore caused some blistering when heated over an open flame. Note that Comparative Example 3 using a partially saponified polyvinyl alcohol has poor Z-axis strength and extremely poor air permeability, resulting in significant blistering. Furthermore, when polyvinyl alcohol is used, whether it is a completely saponified product or a partially saponified product, there is a drawback that the releasability from the drying roll when drying size paper is poor. Example 2 A monomethyl maleate-vinyl acetate copolymer with a monomethyl maleate content of 10.0 mol% was once saponified in a methanol solvent in the presence of a caustic soda catalyst to obtain monomethyl maleate-vinyl acetate with a degree of saponification of vinyl acetate units of 90.0 mol%. - After obtaining vinyl alcohol copolymer particles, sprinkle a 40% caustic soda aqueous solution on the particles, and then uniformly mix with a Henschel mixer to obtain 9.0 mol% of disodium maleate units, 1.0 mol% of monomethyl maleate units, and acetic acid. A saponified copolymer with a degree of saponification of vinyl units of 99.5 mol% was obtained. This saponified copolymer was heated and dissolved in water to prepare a 3% aqueous solution, and Example 1
Size press was performed in the same manner as above. Control Example 4 The saponified product in the first stage in Example 1, that is, the monomethyl maleate-vinyl acetate-vinyl alcohol copolymer 3 with a monomethyl maleate content of 3.0 mol% and a degree of saponification of vinyl acetate units of 95.0 mol%.
Size press was carried out in the same manner as in Example 1 using a % aqueous solution. Example 3 A monobutyl maleate-vinyl acetate copolymer having a monobutyl maleate content of 5.0 mol% was first saponified in methanol and then in water in the presence of a caustic soda catalyst to obtain disodium maleate units.
A saponified copolymer was obtained with a degree of saponification of 4.8 mol%, monobutyl maleate units: 0.2 mol%, and vinyl acetate units: 99.5 mol%. 3 of this saponified copolymer
Size press was carried out in the same manner as in Example 1 using a % aqueous solution. Example 4 A monomethyl maleate-vinyl acetate copolymer having a monomethyl maleate content of 3.0 mol % was obtained by polymerizing maleic anhydride and vinyl acetate in methanol. Maleic anhydride is converted into monomethyl maleate units in the polymer. Next, this copolymer was saponified first in methanol and then in water using a caustic soda catalyst to obtain a copolymer having a degree of saponification of 3.0 mol% of disodium maleate units and 99.7 mol% of vinyl acetate units. Size pressing was carried out in the same manner as in Example 1 using a 3% aqueous solution of this copolymer. The results of Examples 2 to 4 and Control Example 4 are shown in Table 2.

【表】 第2表からも明らかなように実施例2〜4にお
いては実施例1と同様の良好な結果が得られる
が、マレイン酸単位がジナトリウム塩型に変換し
ていず酢酸ビニル単位のケン化度もやや低い対照
例4においては、透気性が劣るため直火加熱に対
し火ぶくれ現象を起す。
[Table] As is clear from Table 2, good results similar to those in Example 1 are obtained in Examples 2 to 4, but the maleic acid units are not converted to the disodium salt type and the vinyl acetate units are In Control Example 4, which has a slightly lower degree of saponification, the air permeability is poor, and a blistering phenomenon occurs when heated over a direct flame.

Claims (1)

【特許請求の範囲】[Claims] 1 マレイン酸エステル―酢酸ビニル共重合体ケ
ン化物を更にアルカリ水溶液の存在下で二次ケン
化して得られるマレイン酸ジアルカリ塩単位0.5
〜20モル%、酢酸ビニル単位のケン化度97モル%
以上のケン化物の水溶液を用いることを特徴とす
るオフセツト輪転印刷用原紙の表面サイズ剤。
1 Maleic acid dialkali salt unit 0.5 obtained by secondary saponification of the maleic acid ester-vinyl acetate copolymer saponified product in the presence of an alkaline aqueous solution
~20 mol%, saponification degree of vinyl acetate unit 97 mol%
A surface sizing agent for base paper for offset rotary printing, characterized in that an aqueous solution of the above saponified substance is used.
JP5347977A 1977-05-09 1977-05-09 Surface sizing method of paper Granted JPS53139811A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5347977A JPS53139811A (en) 1977-05-09 1977-05-09 Surface sizing method of paper

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5347977A JPS53139811A (en) 1977-05-09 1977-05-09 Surface sizing method of paper

Publications (2)

Publication Number Publication Date
JPS53139811A JPS53139811A (en) 1978-12-06
JPS6228239B2 true JPS6228239B2 (en) 1987-06-18

Family

ID=12943972

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5347977A Granted JPS53139811A (en) 1977-05-09 1977-05-09 Surface sizing method of paper

Country Status (1)

Country Link
JP (1) JPS53139811A (en)

Also Published As

Publication number Publication date
JPS53139811A (en) 1978-12-06

Similar Documents

Publication Publication Date Title
US5608011A (en) Crosslinkable polymer powder compositions
US2808381A (en) Resin-dextrin compositions and method of preparation
CA2144792C (en) Aqueous emulsion
CN102958954A (en) Alkyl-modified vinyl alcohol polymer, and composition, thickener, coating material for paper, coated paper, adhesive and film that contain same
JPS6228239B2 (en)
JP3271294B2 (en) Aqueous emulsion and easily disaggregated moisture-proof paper
AU2001266493B2 (en) Use of alkylhydroxyalkyl cellulose possibly in combination with a carboxymethyl cellulose for the improvement of gloss and printability
JPH11140793A (en) Coating-liquid additive for coated paper
JPH0255742A (en) Preparation of foamed polyvinyl alcohol film
JP3769380B2 (en) Polyvinyl alcohol paper coating agent with excellent high-speed coating properties
TWI696670B (en) Coating agent, adhesive and coating
JPH0663199B2 (en) Pigment coating composition for paper
JP2006526084A (en) Use of silane-functional polyvinyl alcohol in primer for release paper and release film
JPH0559689A (en) Sizing agent for paper and paper sized therewith
JPH10259285A (en) Coating agent for paper
US5376447A (en) Wallcovering material containing prepaste adhesives
JPS5936957B2 (en) Rewet hot melt adhesive composition
JPH04103653A (en) Resin composition, adhesive and bonding
JPH09208786A (en) Polyvinyl alcohol resin composition and paper coating agent using the same
JPH08283682A (en) Adhesive
JPS6215678B2 (en)
JPH10298897A (en) Coating agent for paper
JPH04239085A (en) Adhesive
JPS6243447B2 (en)
JP3769351B2 (en) COATING AGENT FOR PAPER AND METHOD FOR PRODUCING COATED PAPER USING THE SAME