JPS5836452A - Water absorbing sheet and its manufacture - Google Patents
Water absorbing sheet and its manufactureInfo
- Publication number
- JPS5836452A JPS5836452A JP56135026A JP13502681A JPS5836452A JP S5836452 A JPS5836452 A JP S5836452A JP 56135026 A JP56135026 A JP 56135026A JP 13502681 A JP13502681 A JP 13502681A JP S5836452 A JPS5836452 A JP S5836452A
- Authority
- JP
- Japan
- Prior art keywords
- water
- sheet
- absorbent
- nozzle
- amount
- 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.)
- Pending
Links
Landscapes
- Laminated Bodies (AREA)
- Paper (AREA)
- Absorbent Articles And Supports Therefor (AREA)
- Lining Or Joining Of Plastics Or The Like (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
本発明は水吸収性シート及びその製造方法に関し、更に
詳しくは少なくとも一方が水浸透性シートである2枚の
シート間に高分子吸収剤を挿入してなる水吸収性シート
に於て、咳高分子吸収剤の脱落がなく、且つ柔軟性に富
む水吸収性シート及びかかるシートを経済的に製造する
ための製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a water-absorbent sheet and a method for producing the same, and more specifically to a water-absorbent sheet formed by inserting a polymer absorbent between two sheets, at least one of which is a water-permeable sheet. The present invention relates to a water-absorbing sheet that does not cause cough polymer absorbent to fall off and is highly flexible, and a manufacturing method for economically manufacturing such a sheet.
高分子吸収剤即ちポリアクリル酸系重合物、OMO,澱
粉誘導体等の吸水性高分子物質の粒状もしくは短繊維状
のものは、吸収材として少なくとも一方が水浸透性シー
トである2枚のシート間に挿入され°C生理用品、紙オ
ムツ尋の衛生製品に用いられている0骸高分子吸収剤を
脱落なく水吸収性シートにて安定Kijl定化する方法
は、一方のシートに該高分子吸収剤を散布後、他方のシ
ートを合せ、エンボス加工する一般に総称される乾式法
、或いは上記方法にて、エンボス加工する前、もしくは
後に若干の水分を付与して、高分子吸収剤の基本特性で
ある水分によるゲル化する特性を利用して加工する一般
に総称される湿式法が考えられる。湿式法による加工は
、為分子吸収剤の基本特性である水分によるゲル化特性
を発現させ、咳高分子吸収剤のゲル化によシ、接着機能
を有す特性から該高分子吸収剤を水吸収性シート内にて
脱落なく固定化する方法としては、適切である@
湿式法にて、鉄水吸収性シートを加工すゐKは、水散布
システムを生理用品並びに紙オムツ等の製品加工機内に
組入れる方法即ち1n−4in・法もしくは、専用にて
水散布による該水吸収性シートを製造する。ff −1
1n・法の2通シが考えられる。A polymer absorbent, that is, a granular or short fibrous water-absorbing polymer material such as a polyacrylic acid polymer, OMO, or a starch derivative, is used as an absorbent between two sheets, at least one of which is a water-permeable sheet. The method of stably stabilizing the zero-carrying polymer absorbent used in sanitary products and sanitary products such as disposable diapers by inserting it into a water absorbent sheet without falling off is to insert the polymer absorbent into one sheet. After spraying the agent, the other sheet is combined and embossed, which is generally called a dry method, or by using the above method, a small amount of moisture is added before or after embossing, and the basic characteristics of the polymer absorbent are applied. Wet methods, which are commonly referred to as processing methods that take advantage of the property of gelling due to certain moisture, are considered. Processing using the wet method allows the polymer absorbent to exhibit its gelation property due to water, which is a basic property of the polymer absorbent. This is an appropriate method for immobilizing iron water absorbent sheets within the absorbent sheet without falling off.@K uses the wet method to process iron water absorbent sheets. The water-absorbing sheet is manufactured by a method of incorporating it into a 1n-4in method, or by a special method of spraying water. ff −1
There are two possible cases: 1n/Law.
湿式法にて、経済性があり、且つ柔軟なる水吸収性シー
トを製造するには、原則的には1n−une法にて行う
事、更に水散布量を該高分子吸収剤を固定するに必要最
低限なる量にて行い、高分子吸収剤の膨潤過多による水
吸収性シートの柔軟性低下をふせぎ、且つ工程的にも、
乾燥工程を必要としない方法が適切といえる。咳湿式法
による加工はスプレー法で、特開@54−125’19
5号公報(三菱レー冒ン)、特開昭51−40497号
公報(ユニチャーム)、特開昭54−1410?を号公
報にて開示されているが、いずれの発明も装置的には、
off−14n・の形式をとっている。In order to produce an economical and flexible water absorbent sheet using a wet method, the 1n-une method should be used in principle, and the amount of water sprayed should be adjusted to fix the polymer absorbent. This is done in the minimum necessary amount to prevent the decrease in flexibility of the water absorbent sheet due to excessive swelling of the polymer absorbent, and also from a process standpoint.
A method that does not require a drying step is considered appropriate. Processing using the cough wet method is a spray method, published in Japanese Patent Publication No. 54-125'19.
Publication No. 5 (Mitsubishi Ren), Japanese Patent Application Laid-open No. 51-40497 (Unicharm), Japanese Patent Application Publication No. 1410-1982? However, both inventions are device-wise,
It takes the form of off-14n.
水散布なるスプレー法は、水散布量をある定条下に於て
、一定量散布するととは可能であり、更に水通時に、加
工機(1n−1ineの場合に於て、生理用品、オムツ
等の生産機)もしくは腋水吸収性シート専用機(0ff
−11noの場合)の生産スピードを一例としてスプレ
ーの内圧変化と連動する事によシ、水吸収性シート自体
に定常的に一定量散布する事も可能である事から原理的
には可能である。In the spray method called water spraying, it is possible to spray a fixed amount of water under a certain fixed line. etc. production machine) or a dedicated machine for axillary water absorbent sheets (0ff
In principle, it is possible to spray a constant amount onto the water-absorbing sheet itself by linking the production speed with the change in the internal pressure of the spray (for example, in the case of -11no). .
しかし、水散布の対象となる一定量の水吸収性シー)K
水を散布する上に於て、母機(加工機4しくは専用機)
との生産スピードとスプレーの内圧とを連動させ、水の
散布量を一定にコントロールさせる際に、母機が高速に
なりた時、即ちスプレーの内圧が高くなう走時スプレー
の散布量は拡がシ、水が周囲へ飛散する事になる。However, a certain amount of water-absorbing sea) K which is subject to water spraying
When spraying water, the main machine (processing machine 4 or special machine)
When controlling the amount of water sprayed at a constant level by linking the production speed with the internal pressure of the sprayer, when the mother machine becomes faster, that is, the internal pressure of the sprayer increases, and the amount of sprayed water spreads. Yes, water will be scattered around.
従って核問題に対処すべくスプレーの高さを調節する事
によシ、散布量を制御する事は可能であるが、装置的に
大がかりとなる。又スプレー散布は、水を噴霧状に散布
する事となシ、水滴の周囲への飛散となシ、周囲飛散防
止のカバーを取付けても、水滴の凝集要因となり、機械
上の対処が必要である。父母機が何らかの事故にて、瞬
時に停止した場合、スプレー内の残圧によシスプレーI
IcW4留している水滴がボタ落ちし、水吸収性シート
への散布量が所定量ニジ多くなる。上記のスプレーの水
散布量自体の制御性から該水吸収性シートに水散布後乾
燥機が必要となり、装置上、経済性の面で問題となる。Therefore, in order to deal with the nuclear problem, it is possible to control the amount of spray by adjusting the height of the spray, but this requires a large-scale equipment. In addition, spraying does not spray water in the form of a mist, and does not allow water droplets to scatter around the area.Even if a cover is installed to prevent scattering, it may cause water droplets to aggregate, and mechanical measures are required. be. If the parent unit suddenly stops due to some kind of accident, the system spray I will be activated due to the residual pressure in the sprayer.
The water droplets remaining in IcW4 drip off, and the amount of water sprayed onto the water absorbent sheet increases by a predetermined amount. Because of the controllability of the water spray amount itself, a dryer is required after water is sprayed on the water absorbent sheet, which poses problems in terms of equipment and economic efficiency.
本発明者らは上記の問題を背景に種々検討した結果、該
所定水吸収性シート巾に正確に水を散布し、且つ所定水
吸収性シート内の高分子吸収剤を安定に固定すべく、最
少の有効水散布量を精度よく散布出来、該水吸収性シー
ト加工上に於て、咳加工工程内に乾燥機を導入する必要
のない極めて経済性ある水散商法技術を完成し、本発明
に至った。The present inventors have conducted various studies based on the above-mentioned problems, and have found that in order to accurately spray water over the width of the predetermined water-absorbent sheet and stably fix the polymer absorbent within the predetermined water-absorbent sheet, The present invention has completed an extremely economical water sprinkling method that can spray the minimum amount of effective water with high accuracy and does not require the introduction of a dryer into the cough processing process when processing the water-absorbent sheet. reached.
即ち、本発明は可撓性である第1のシートと可撓性且つ
水浸透性である第2のシートの間に吸水性高分子物質を
挾持させ、水を柱状流状態にて付加してなる水吸収性シ
ート及び可撓性である第1のシートの上Kll水性高分
子物質を散布し、更に可撓性且つ水浸透性である第2の
シートで覆って水吸収性シートを製造するに際し、水を
ノズルから柱状流状態にて付加することを特徴とする水
吸収性シートの製造方法を提供するものである。That is, in the present invention, a water-absorbing polymer substance is sandwiched between a flexible first sheet and a flexible and water-permeable second sheet, and water is added in a columnar flow state. A water-absorbent sheet is prepared by spraying a Kll water-based polymer material on a flexible first sheet and covering it with a flexible and water-permeable second sheet. The present invention provides a method for producing a water-absorbing sheet, characterized in that water is added in a columnar flow state from a nozzle.
以下、図面により本発明を更に詳細に説明するO
第1図及び第2図に本発明に用いられるノズルの例を示
す。第1図は針状ノズル1の断面図、第2図は円板状ノ
ズル4の断面図である。ここで2は水注入口、5は水吐
出口である。この様な柱状流にて水を散布可能なるノズ
ルを第5図に示すノズルヘッド5に装着する。ここで6
はパツキン、7はノズル装着部である。第4図に円板状
ノズル4をノズルヘッド5に装着した状態を示す0トζ
で8はストレイナーである。咳ノズル4を装着したノズ
ルヘッド5による水散布状況は、第5図に示す状態とな
る。Hereinafter, the present invention will be explained in more detail with reference to the drawings. Figs. 1 and 2 show examples of nozzles used in the present invention. FIG. 1 is a cross-sectional view of the needle-shaped nozzle 1, and FIG. 2 is a cross-sectional view of the disk-shaped nozzle 4. Here, 2 is a water inlet, and 5 is a water outlet. A nozzle capable of spraying water in such a columnar flow is attached to a nozzle head 5 shown in FIG. 5. here 6
7 is a packing, and 7 is a nozzle mounting part. Figure 4 shows the disk-shaped nozzle 4 attached to the nozzle head 5.
8 is a strainer. The state of water spraying by the nozzle head 5 equipped with the cough nozzle 4 is as shown in FIG.
核力式によれば、水の散布は、第1図もしくは第2図に
示すようなノズルのオリフィス状構造から柱状流10と
なシ、スプレーによシみられる噴霧状での水飛散は問題
にならない。又散布量は、ノズルヘッド5の巾にて固定
され、ノズルヘッド5内の内圧変化があっても、スプレ
ーにてみられる様な変動はない。従ってノズルヘッドの
巾を、散布対象吸収体中と同一にすれば、たえず吸収体
への均一散布となる。According to the nuclear force formula, water is distributed in a columnar flow 10 from the orifice-like structure of the nozzle as shown in Figure 1 or Figure 2, and water scattering in the form of a mist seen in spraying is a problem. do not become. Furthermore, the amount of spraying is fixed across the width of the nozzle head 5, and even if the internal pressure within the nozzle head 5 changes, there is no variation as seen in sprays. Therefore, if the width of the nozzle head is made the same as the width of the absorbent body to be sprayed, uniform spraying on the absorbent body will be achieved.
一方蚊ノズルにて散布すると、吸収体への水散布軌跡は
、散布−瞬にて線状なる軌跡となるも、吸収体表層にて
、水の拡散が生じ、その結果均一に水を散布した状態、
即ち第5図の水吸収性シート11への軌跡12の状態と
なる。On the other hand, when spraying with a mosquito nozzle, the trajectory of water sprayed onto the absorbent body becomes a linear trajectory at the moment of spraying, but water spreads on the surface layer of the absorbent body, and as a result, water is sprayed uniformly. situation,
That is, the state is the trajectory 12 toward the water absorbent sheet 11 shown in FIG.
ノズルヘッド5から散布対象となる吸収体の高さは、該
ノズルによる水の安定なる柱状流を得るため、5 m/
m 〜300 m/m位迄が好マシイ〇更に該散布にと
もなう水送附方式は、母機の加エスピー″ドに相応して
、水の散布量をコントロールする制御性の面から、加圧
方式もしくはギヤーポンプ等の定量ポンプ方式が好まし
い。The height of the absorber to be sprayed from the nozzle head 5 is set at 5 m/cm in order to obtain a stable columnar flow of water through the nozzle.
m ~ 300 m/m is preferable 〇 Furthermore, the water delivery method accompanying the spraying is a pressurized method from the viewpoint of controllability that controls the amount of water sprayed according to the application speed of the mother machine. Alternatively, a metering pump system such as a gear pump is preferable.
加圧方式は、母機の加ニスピード即ちモーター回転スピ
ードの信号を取出し、該電気信号を空気圧に変換し、回
転スピードに準じた加圧空気を貯水した加圧タンクに送
シ込み、該加圧に準じた水を水注入パイプ9により、上
記第1図もしくは第2図に示すようなノズルを装着した
ノズルヘッド5に送シ込み、その結果、母機の加ニスピ
ードと相応した水の量の散布となる。又定量ポンプ方式
は、定量ポンプの回転スピードを母機の回転スピードと
連動させ、その結果該定量ポンプにて貯水タンクよシ汲
み出された水を水注入パイプ9により第1図もしくは、
第2図に示すような一ノズルを装着したノズルヘッド5
に送シ込み、母機の加ニスピードと相応した水の量の散
布となる。第6図は加圧方式にて水を送附した時の空気
圧、即ち吐出圧と水吐出量との相関を図示したもので、
−例として口径120μφ、N@e+11e長27 m
/mなる第1図に示す針状ノズル1を、巾60m/ms
長さ115$m、厚みs o m/mなる第5図に示す
ノズルヘッド5に装着して水を送附した場合である。第
7図は定量ポンプ方式にて、口径80μφ、厚みO,!
in/mなる第2図に示す板状ノズル4を巾60m/!
!1%長さ115m1!E1.厚み50m/mなる第3
図に示すノズルヘッド5に12コ装着して水を送附し九
場会のモーター回転数と水吐出量との相関を図示したも
のである。The pressurization method takes the signal of the motor rotation speed, that is, the motor rotation speed of the mother machine, converts this electrical signal into air pressure, and sends pressurized air according to the rotation speed to a pressurization tank containing water. The water according to the water injection pipe 9 is fed into the nozzle head 5 equipped with a nozzle as shown in Fig. 1 or Fig. It becomes dispersion. Also, in the metering pump system, the rotational speed of the metering pump is linked to the rotational speed of the mother machine, and as a result, the water pumped out from the water storage tank by the metering pump is pumped through the water injection pipe 9 as shown in FIG.
Nozzle head 5 equipped with one nozzle as shown in Fig. 2
The amount of water is sprayed according to the speed of the mother machine. Figure 6 shows the correlation between the air pressure, that is, the discharge pressure, and the amount of water discharged when water is supplied using the pressurized method.
- For example, diameter 120μφ, N@e+11e length 27 m
The needle-shaped nozzle 1 shown in FIG. 1 with a width of 60 m/ms
This is the case when the nozzle head 5 shown in FIG. 5, which has a length of 115 $m and a thickness of s o m/m, is attached to send water. Figure 7 shows a metering pump system with a diameter of 80 μφ and a thickness of O,!
In/m, the plate nozzle 4 shown in FIG. 2 has a width of 60 m/!
! 1% length 115m1! E1. The third layer has a thickness of 50m/m.
This figure illustrates the correlation between the motor rotation speed and the amount of water discharged when 12 nozzles are attached to the nozzle head 5 shown in the figure to send water.
いずれも水の吐出量と、母機とのスピードの連動性に於
て、線型の相関があり、水の吐出量の制御性に於て優れ
ている事がわかる。In both cases, there is a linear correlation between the amount of water discharged and the speed with the mother machine, and it can be seen that the controllability of the amount of water discharged is excellent.
一方、該水吸収性シートに於て咳高分子吸収剤を脱落な
く、安定に固定し、且つ柔軟なるシートを得るための水
散布量の条件は、高分子吸収剤を若干膨潤させ、且つ蚊
状態での高分子吸収剤を介在させて、上層、下層のシー
トを接合させるための最少め水散布量(Twin)と、
更に咳高分子吸収剤が、水吸収し死時、蚊高分子の特性
である咳高分子構造内水をかかえ込み、吸水後、加圧し
ても水を離さない限界(Wmax )内にて行う必要が
ある。一般に高分子吸収剤といわれる吸収剤の特性とし
て、若干の水分にて、安定な膨潤挙動を示し、自重の数
十倍に及び飽和での吸収状態にて湿潤を示す膨潤挙動と
なる。On the other hand, in order to stably fix the cough polymer absorbent in the water absorbent sheet without falling off and to obtain a flexible sheet, the conditions for the amount of water sprayed are such that the polymer absorbent is slightly swollen and mosquito The minimum amount of water sprayed (Twin) for joining the upper and lower sheets with a polymer absorbent interposed in the state,
Furthermore, when the cough polymer absorbent absorbs water and dies, it retains the water within the cough polymer structure, which is a characteristic of mosquito polymers, and after absorbing water, it is necessary to do so within the limit (Wmax) that does not release water even when pressurized. There is. The characteristics of the absorbent, which is generally referred to as a polymer absorbent, is that it exhibits stable swelling behavior in the presence of a small amount of water, and exhibits wet swelling behavior in a saturated state of absorption of several tens of times its own weight.
又、咳水吸収性シートの構成下に於て、皺高分子吸収剤
飽和吸収量以下の水を散布すると、高分子吸収剤の吸収
力により吸収紙等に介在する水を積極的に吸収し、該水
吸収シート全体がほとんど湿けを示さない、乾燥状態な
る特性を示す。In addition, in the structure of the cough water absorbent sheet, if water is sprayed below the saturated absorption capacity of the wrinkled polymer absorbent, the absorbing power of the polymer absorbent will actively absorb the water present in the absorbent paper, etc. , the entire water-absorbing sheet shows almost no moisture, exhibiting the characteristic of being in a dry state.
上記これらの特性を利用して、腋高分子吸収剤を含む鉄
水吸収性シー)K於て、水散布量のtwinとWmax
なる限界は該高分子吸収剤散布機)10−〜70sであ
れば良い。即ち、本発明に於ける鎖高分子吸収剤を含む
水吸収性シートを性能上、高分子吸収剤の脱落なく、安
定にして且つ柔軟なる水吸収性シートを得、且つ一方誼
水吸収性シート加工工程内にて、乾燥機の導入をともな
わない極めて経済性ある加工技術は、上記高分子吸収剤
の対水挙動にあった制御されたろ水散布法を必要とする
。一方が少なくとも親水性なる鉄水吸収性シートに於て
、該親水性シート側よシ散布された上記水散布量は、該
水吸収性シートに含まれる高分子吸収剤を若干膨潤させ
、tI温調時て腋水吸収性シートを構成する上層、下層
を接合して安定な水吸収性シートの形成となシ、更に高
分子吸収剤の水吸収の進展に伴い、結果的に該水吸収性
シートをはとんど湿潤しえない状態にて形成せしめる事
が出来る。Utilizing these characteristics mentioned above, in the iron water absorbent sheet containing the armpit polymer absorbent, the twin and Wmax of the water spray amount can be adjusted.
The limit is 10 to 70 seconds (for the polymer absorbent sprayer). That is, in terms of performance, the water-absorbent sheet containing a chain polymer absorbent according to the present invention can be made stable and flexible without shedding of the polymer absorbent, and at the same time, the water-absorbent sheet can be made flexible. A highly economical processing technique that does not involve the introduction of a dryer in the processing process requires a controlled water distribution method that matches the water behavior of the polymeric absorbent. In an iron water-absorbing sheet where one side is at least hydrophilic, the amount of water sprayed from the hydrophilic sheet side slightly swells the polymeric absorbent contained in the water-absorbing sheet and causes the tI temperature to rise. The upper and lower layers that make up the axillary water-absorbent sheet are bonded together at the appropriate time to form a stable water-absorbent sheet, and as the water absorption of the polymer absorbent progresses, the water-absorbent properties The sheet can be formed in a state where it can hardly be wetted.
第1図及び第2図に示される形状の水柱流散布可能なる
ノズルの形状に於て、吐出口3の大きさ並びに第1図で
の針長は、水散布量に依存するが、第8図に示す如く、
ノズルヘッド圧をパラメーターとしてノズル口径と該ノ
ズル口径にて吐出する水の量とは相関を示す。ここで1
はヘッド圧0 、2 %/ Om2の場合、bはヘッド
圧0.・410n”の場合、Cはヘッド圧2 、 OI
c970m”の場合である。従って、所要の水散布量に
於て、%にノズルの口径、並びに針長にての制限を必要
としないが、ノズルの直径が0.O5mm 〜0.2
mmの範囲内のものが好ましい。In the shape of the nozzle capable of water column spraying as shown in FIGS. 1 and 2, the size of the discharge port 3 and the needle length in FIG. 1 depend on the amount of water sprayed. As shown in the figure,
There is a correlation between the nozzle diameter and the amount of water discharged through the nozzle diameter using the nozzle head pressure as a parameter. Here 1
is when the head pressure is 0.2%/Om2, and b is when the head pressure is 0.2%/Om2.・For 410n”, C is head pressure 2, OI
Therefore, there is no need to limit the required water spray amount by the nozzle diameter or needle length, but if the nozzle diameter is 0.05mm to 0.2mm.
Preferably, it is within the range of mm.
水散布場所は、第9図に示す加工機上において、該高分
子吸収剤散布機19の前もしくは後の水浸透性又は水不
浸透性シート16上もしくは上層を水浸透性シート、下
層を水浸透性又は水不浸透性シートとし、これらの関に
該高分子吸収剤を挿入後のシート上に於て散布するかい
ずれの場合も嵐い。The water spraying location is on the processing machine shown in FIG. A permeable or water-impermeable sheet may be used, and the polymeric absorbent may be sprayed onto the sheet after insertion.
父上層を水浸透性シート、下層を水浸透性もしくは水不
浸透性シートとし、これらの間に咳高分子吸収剤を挿入
した後、必要あれば若干のプレス圧なるプレス四−ル2
01’14に該水吸収性シートを導入すれば、より安定
な水吸収性シートが得られ、水散布場所を、該加圧ロー
ルの後に設けてもよい。具体的には、第9図に示す加工
機上、水散布可能場所は21.22,2!5いずれでも
喪いが、好ましくは22.25である。The upper layer is a water-permeable sheet, the lower layer is a water-permeable or water-impermeable sheet, and after inserting a cough polymer absorbent between them, press four with a slight press pressure if necessary.
If the water-absorbent sheet is introduced in 01'14, a more stable water-absorbent sheet can be obtained, and the water spraying location may be provided after the pressure roll. Specifically, on the processing machine shown in FIG. 9, water can be sprayed at either 21.22 or 2!5, but preferably 22.25.
l′i!d該プレス上プレス、もしくはエンボスロール
いずれの形式のものでも良い。l'i! (d) Either a press on the press or an embossing roll may be used.
以下、実施例によ抄本発明を更に詳細に説明する。Hereinafter, the present invention will be explained in more detail with reference to Examples.
実施例1
第10図の直線dなる母機スピードと水散布量の条件下
、即ち、口径70μ、板厚100μなる第2図に示す形
状のノズルを、巾70 m/m 。Example 1 A nozzle having the shape shown in FIG. 2 with a diameter of 70 μm and a plate thickness of 100 μm was used to have a width of 70 m/m under the conditions of the mother machine speed and water spray amount as indicated by the straight line d in FIG. 10.
長さb o m/m s厚み50m/IIなる第5図に
示すノズルヘッドに110本装着し、加圧方式にてへy
Y 圧0 、2 b/am” O’Jk 件下テ、I
付S 1 t/Wl” %クレープ率40惨、巾70
m/mの水浸透性シート上に、ポリアクリル酸系高分
子吸収剤(化工石鹸製4ワンダーゼエル″′)を17炉
/−S−に散布後、上記同一水浸透性シートを会せ、加
圧1KI/Cml1のプレスローラー間に導入後のシー
ト上に水散布を行った0その結果表−1のAIK示す、
高分子吸収剤の脱落ない、且つ柔軟なる極めて、安定な
水吸収性シートを得九。向上加工条件下での水散布量は
鋏高分子吸収剤当り14重量−となり、水散布状況は、
安定なる柱状流下で且つ、周囲に全く水飛散のない状態
であった0
実施例−2
第10図の直線fなる母機スピードと、水散布量の条件
下、即ち第1図に示す口径140μ、針長27m/mの
ノズルを18本第5図に示す中200 Vm、長さ60
m/m s厚みs o m/mのノズルヘッドに装着
し、加圧方式にてヘッド圧1.6麺10− の条件下で
、目付55 f / m” sクレープ率StSなる中
200m/mの耐水シート上に、アクリル酸と澱粉共重
合体系高分子吸収剤(三洋化■ I
成製 サンウェット )を26 f / IEI均一
に散布後、実施例1で用いたものと同じ水浸透性シート
を合せた上に水を散布し、その後加圧1−/−の上部エ
ンボスロー2−なる加圧ローラー関に導入した。110 nozzles were attached to the nozzle head shown in Fig. 5 with a length of b o m/m and a thickness of 50 m/II, and were heated using a pressurizing method.
Y pressure 0, 2 b/am” O'Jk condition, I
Attached S 1t/Wl” % crepe rate 40%, width 70
After spraying polyacrylic acid-based polymer absorbent (4 Wonder Zeel'' made by Chemical Soap Co., Ltd.) on a water-permeable sheet of m/m in 17 furnace/-S-, the same water-permeable sheet was put together and processed. Water was sprayed on the sheet after introduction between press rollers with a pressure of 1 KI/Cml 1. The results are shown in Table 1 with AIK.
An extremely stable water-absorbing sheet which is flexible and does not have the polymer absorbent falling off is obtained. The amount of water sprayed under the improved processing conditions was 14% by weight per scissors polymer absorbent, and the water spraying situation was as follows:
It was a stable columnar flow and there was no water scattering around it.Example-2 Under the conditions of the mother machine speed and the water spray amount as shown in the straight line f in Fig. 10, that is, the diameter of 140μ as shown in Fig. 1, 18 nozzles with a needle length of 27 m/m as shown in Figure 5, medium 200 Vm, length 60
When attached to a nozzle head with a thickness of m/m and a head pressure of 1.6 m/m using a pressurizing method, the crepe rate StS is 200 m/m. After uniformly spraying acrylic acid and starch copolymer-based polymer absorbent (Sunwet, manufactured by Sanyo Kaisha, Ltd.) at 26 f/IEI onto a water-resistant sheet, the same water-permeable sheet as used in Example 1 was applied. Water was sprinkled on top of the mixture, and then introduced into a pressure roller having an upper embossing throw of 2-/- with a pressure of 1-/-.
その結果1!−1の42に示す、高分子脱落のない、且
つ柔軟な極めて安定なる水吸収性シートを得た。同tX
条件下での水散布量は、咳高分子吸収剤当F)481g
となシ、水散布状況は、安定なる柱状流下で且つ、周囲
に全く水飛散のない状態であった〇
実施例−5
第10図の直線のなる母機スピードと、水散布量の条件
下、即ち口径80μ、厚さ100μなる第2図に示す形
状のノズル12コを巾70m/m。The result is 1! A flexible and extremely stable water-absorbing sheet with no polymer shedding was obtained as shown in No. 42 of -1. Same tX
The amount of water sprayed under the conditions is 481g of cough polymer absorbent (F)
The water spraying situation was a stable columnar flow with no water splashing around. Example 5 Under the conditions of the mother machine speed and the water spray amount as shown in the straight line in Figure 10, That is, 12 nozzles having a diameter of 80 μm and a thickness of 100 μm and having the shape shown in FIG. 2 were used with a width of 70 m/m.
長さ60t/ms厚さ50t/mなる第3図に示すノズ
ルヘッドに装着し、定量ポンプ方式による水送附条件下
で、目付51t/m” 、クレープ率40チ、巾y o
m/mの水浸透性シート上に、ポリアクリル酸系高分
子吸収剤(化工石鹸製のワンダーゼエル)を100f/
八−に散布後、上記同一水浸透性シートを合せ、加圧1
1Ey/ all” のプレスローラー間に導入後のp
)上に水散布を行った。It was attached to the nozzle head shown in Fig. 3 with a length of 60 t/ms and a thickness of 50 t/m, and under the conditions of water supply using a metering pump method, the fabric weight was 51 t/m'', the crepe rate was 40 inches, and the width was y o.
100 f/m of polyacrylic acid-based polymer absorbent (Wonder Zeel manufactured by Chemical Soap) on a water-permeable sheet of m/m.
After spraying on step 8, put the same water permeable sheet above together and pressurize 1.
p after introduction between 1Ey/all” press rollers
) was sprayed with water.
その結果表−1のム5に示す、高分子吸収剤の脱落ない
且つ柔軟な極めて安定なる水吸収性シーFを得た。As a result, a flexible and extremely stable water-absorbing sheet F without the polymer absorbent falling off was obtained as shown in column 5 of Table 1.
同、蚊水散布条件は、定量ポンプ回転数を母機のスピー
ドに連動させ、水散布量50 oo/mlnは定量ポン
プ回転数475 Orpmに対応させ丸〇又該水散布量
は高分子吸収剤当り30−となり、水散布状況は、安定
なる柱状流下で且つ周囲に全く飛散のない状態であった
。The mosquito water spraying conditions are as follows: The metering pump rotation speed is linked to the speed of the base machine, and the water spray amount of 50 oo/ml corresponds to the metering pump rotation speed of 475 orpm.The water spray amount is also per polymer absorbent. 30-, and the water spraying condition was a stable columnar flow with no scattering around the area.
比較例1 (ウェット法; off −1ineにて、
スプレー法による水吸収性シートの製造)目付31f/
!I2、クレープ率40%、巾500xy’mの水浸透
性シート上に、ポリアクリル酸系高分子吸収剤(化工石
鹸製′■ワンダーゼエル′ )を17t/−均一に散布
し、上記同一水浸透性シートを合せ、加圧1即10−の
プレスロー2−間に導入後、スプレーノズルにて7Bt
/m”、該高分子吸収割当シ!1001gの水を散布後
、温R130℃、長さ2mlの乾燥機にて、乾燥する事
により水吸収性シートを得九〇両胸ニスビードは2Qm
/winでありた。得られたシートの物性を実施例1と
同様に評価し、結果を表−1に示した。Comparative example 1 (wet method; off -1ine,
Manufacture of water absorbent sheet by spray method) Fabric weight: 31f/
! I2. On a water-permeable sheet with a crepe rate of 40% and a width of 500xy'm, 17 tons/- of a polyacrylic acid-based polymer absorbent ('Wonder Zell' manufactured by Kako Soap) was uniformly sprinkled, and the same water permeability as above was obtained. After putting the sheets together and introducing them between the press rows of 1 and 10, 7Bt was applied with a spray nozzle.
/m", the polymer absorption capacity! After spraying 1001g of water, dry it in a dryer with a temperature of 130℃ and a length of 2ml to obtain a water-absorbent sheet. 90 breast varnish beads are 2Qm
/It was a win. The physical properties of the obtained sheet were evaluated in the same manner as in Example 1, and the results are shown in Table 1.
比較例2 (ドライ法; 1fi−1in@にて、プレ
スローラーのみKよる水吸収性シートの製造)目付s
1t/j’、クレープ率4096、巾70m7’rnの
水浸透性シート上に、ポリアクリル酸系高分子吸収剤(
化工石鹸製の′ワンダーゼエル1 )を17f/−均一
に散布し、上記同一水浸透性シートを合せ、一方が温度
180℃に加温され、且り加圧2.sW4/+−なる加
圧ローラー間に導入して水吸収性シートを得九。両胸ニ
スピードは60ル/wimであった。得られ九シートの
物性を実施例1と同様に評価し、結果を表−1に示した
。Comparative Example 2 (Dry method; Manufacture of water absorbent sheet using only press roller K at 1fi-1in@) Area weight s
A polyacrylic acid-based polymer absorbent (
Wonder Zeel 1) made from chemical soap was uniformly spread at 17 f/-, and the same water-permeable sheets described above were put together, one side was heated to 180°C, and pressurized 2. sW4/+- to obtain a water absorbent sheet between pressure rollers. The speed between both breasts was 60 ru/wim. The physical properties of the obtained nine sheets were evaluated in the same manner as in Example 1, and the results are shown in Table 1.
表−1 注) 中1 柔軟性;カンチレバー法による。Table-1 Note) Middle 1 Flexibility: Based on the cantilever method.
第11図に示すように水吸収性シー
ト24(巾70!l/IIIX長さ170をへ)を台2
5上にて一定速度V = S mrs/seaでスライ
ドさせ、斜面と接触し
た時の長さLをもって表示する。L
値が短いほど柔軟である事を示す。As shown in FIG.
5 at a constant speed V = S mrs/sea, and the length L at the time of contact with the slope is displayed. The shorter the L value, the more flexible it is.
ここでθは45°である。Here, θ is 45°.
中2 高分子吸収剤脱落性;シェーカー法による。Medium 2: Removal of polymer absorbent; by shaker method.
第12図に示すように水吸収性シー
ト24(巾70q/mX長さ1yo$m%重量−)をシ
ェーカー装置26(藷
にト臘りエーカー、蓋弐8−L1l)
に取付は矢印27の方向でS分間
goo rpmで振動させた後の水吸収性シート24の
重量W、を測定す
る。As shown in FIG. 12, the water absorbent sheet 24 (width 70q/m x length 1yo$m% weight) is attached to the shaker device 26 (cover 28-L1l) as indicated by the arrow 27. The weight W of the water absorbent sheet 24 after being vibrated in the direction S minutes at goo rpm is measured.
高分子吸収剤脱落量Wetl−Ws 鎖脱落量をもって、・水吸収性シー トの安定性の目安とする。Amount of polymer absorbent falling off Wetl-Ws ・Water-absorbent seams with the amount of chain shedding This is used as a guide to the stability of the target.
第1図は針状ノズルの断面図、第2図は板状ノズルの断
面図、第5図はノズルヘッドの斜視図、第4図は板状ノ
ズルをノズルヘッドに装着した状態を示す断面図、第5
図は本発明方法による水散布状況を示す斜視図、第6図
は水吐出量と吐出圧との相関図、第7図は水吐出量と定
量ポンプのモーター回転数との相関図、第8図はノズル
ヘッド圧をパラメーターとした水吐出量とノズル直径と
の相関図、第9図は加工機上での水散布可能場所を示す
図、第10図は母機スピードと水散布量との相関図、第
11図は柔軟性の評価に用いた装置の略示正面図、第1
2図は高分子吸収剤脱落性の評価に用い九シェーカー装
置の略示正面図である。
1・・・針状ノズル、2中・・水注入口、5・・・水吐
出口、4・・・板状ノズル、5・・・ノズルヘッド、9
・・・水注入パイプ、1o・・・柱状流、11・日永浸
透性シート、I !−・シートロール、16・・・水浸
透性もしくは水不浸透性シート、17・・・ガイドロー
ル、18・・・水散布ノズルヘッド、19・・・高分子
吸収剤散布機、20・・・プレスロール、21,22.
23・・・水散布可能場所
出願人代理人 古 谷 馨第 10
図
0 20 40 60
80母機スピード(m/mtn)
第11図
4Figure 1 is a sectional view of the needle nozzle, Figure 2 is a sectional view of the plate nozzle, Figure 5 is a perspective view of the nozzle head, and Figure 4 is a sectional view of the plate nozzle attached to the nozzle head. , 5th
The figure is a perspective view showing the water spraying situation according to the method of the present invention, Figure 6 is a correlation diagram between water discharge amount and discharge pressure, Figure 7 is a correlation diagram between water discharge volume and metering pump motor rotation speed, and Figure 8 is a correlation diagram between water discharge amount and metering pump motor rotation speed. The figure shows the correlation between water discharge amount and nozzle diameter using nozzle head pressure as a parameter, Figure 9 shows the locations where water can be sprayed on the processing machine, and Figure 10 shows the correlation between base machine speed and water spray amount. Figure 11 is a schematic front view of the device used for evaluating flexibility.
FIG. 2 is a schematic front view of a nine-shaker device used to evaluate the shedding property of a polymer absorbent. 1... Needle nozzle, 2... Water inlet, 5... Water outlet, 4... Plate nozzle, 5... Nozzle head, 9
...Water injection pipe, 1o...Column flow, 11.Hinaga permeable sheet, I! - Sheet roll, 16... Water-permeable or water-impermeable sheet, 17... Guide roll, 18... Water spray nozzle head, 19... Polymer absorbent sprayer, 20... Press roll, 21, 22.
23...Place where water can be sprayed Applicant's agent Kaoru Furuya 10th
Figure 0 20 40 60
80 Mother machine speed (m/mtn) Figure 11 4
Claims (1)
ある第2のシートの間に吸水性高分子物質を挾持させ、
水を柱状流状態にて付加してなる水吸収性シート。 2 水を1lL2のシートの表面から付加してなる特許
請求の範囲第1項記載の水吸収性シート。 5 第1のシートが水浸透性である特許請求の範囲第1
項記載の水吸収性シート0 4 可撓性である第1のシートの上に吸水性高分子物質
を散布し、更に可撓性且つ水浸透性である第2のシート
で覆って水吸収性シートを製造するに際し、水をノズル
から柱状流状態にて付加することを特徴とする水吸収性
シートの製造方法。 5 水を第2のシートの表面から付加する特許請求の範
囲第4項記載の製造方法。 6 水を吸水性高分子物質の重量の10〜70チ付加す
る特許請求の範囲第4項、記載の製造方法。 7 ノズルの直径がo、osmm〜0.2社である特許
請求の範囲第4項記載の製造方法。[Claims] 1. A water-absorbing polymer material is sandwiched between a flexible first sheet and a flexible and water-permeable second sheet,
A water absorbent sheet made by adding water in a columnar flow state. 2. The water absorbent sheet according to claim 1, wherein water is added from the surface of a 1L2 sheet. 5 Claim 1 in which the first sheet is water permeable
Water-absorbing sheet described in Section 0 4 A water-absorbing polymer material is sprinkled on a flexible first sheet, and then covered with a flexible and water-permeable second sheet to absorb water. A method for producing a water absorbent sheet, which comprises adding water in a columnar flow from a nozzle when producing the sheet. 5. The manufacturing method according to claim 4, wherein water is added from the surface of the second sheet. 6. The manufacturing method according to claim 4, wherein water is added in an amount of 10 to 70 times the weight of the water-absorbing polymeric material. 7. The manufacturing method according to claim 4, wherein the nozzle has a diameter of 0, osmm to 0.2.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56135026A JPS5836452A (en) | 1981-08-28 | 1981-08-28 | Water absorbing sheet and its manufacture |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56135026A JPS5836452A (en) | 1981-08-28 | 1981-08-28 | Water absorbing sheet and its manufacture |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS5836452A true JPS5836452A (en) | 1983-03-03 |
Family
ID=15142193
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56135026A Pending JPS5836452A (en) | 1981-08-28 | 1981-08-28 | Water absorbing sheet and its manufacture |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5836452A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01230671A (en) * | 1987-09-21 | 1989-09-14 | Johnson & Johnson Prod Inc | Absorbing hydride and immobilization thereof |
| JPH02193665A (en) * | 1989-01-24 | 1990-07-31 | Oji Paper Co Ltd | Method for producing absorber for throw-away diaper |
-
1981
- 1981-08-28 JP JP56135026A patent/JPS5836452A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01230671A (en) * | 1987-09-21 | 1989-09-14 | Johnson & Johnson Prod Inc | Absorbing hydride and immobilization thereof |
| JPH02193665A (en) * | 1989-01-24 | 1990-07-31 | Oji Paper Co Ltd | Method for producing absorber for throw-away diaper |
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