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JP2009112347A - Absorbent manufacturing method and manufacturing apparatus - Google Patents

Absorbent manufacturing method and manufacturing apparatus Download PDF

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JP2009112347A
JP2009112347A JP2007285479A JP2007285479A JP2009112347A JP 2009112347 A JP2009112347 A JP 2009112347A JP 2007285479 A JP2007285479 A JP 2007285479A JP 2007285479 A JP2007285479 A JP 2007285479A JP 2009112347 A JP2009112347 A JP 2009112347A
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polymer
water
supply pipe
absorbing polymer
duct
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JP5102582B2 (en
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Yasuhiro Umeki
保宏 梅木
Kenji Ando
賢治 安藤
Kenichi Sato
健一 佐藤
Hiroaki Harada
拓明 原田
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Kao Corp
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Kao Corp
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Abstract

【課題】吸収体製造時の流れ方向(MD)に直交する方向(CD)に吸水性ポリマーに均一に分散させることができる吸収体の製造方法及び製造装置を提供すること。
【解決手段】本発明の吸収体の製造方法は、ダクト3内を流れる空気流中にポリマー供給管5を介して吸水性ポリマー51を導入し、該空気流に載せて搬送した吸水性ポリマー51を所定形状に堆積させる工程を具備する吸収体の製造方法であり、圧縮空気の噴射により、前記ポリマー供給管5中の吸水性ポリマー51を加速し、加速した該吸水性ポリマーを、該ポリマー供給管5の先端部又は該ポリマー供給管5の延長線上に設けた分散プレート53に衝突させ、衝突により分散した吸水性ポリマーを前記空気流中に導入する、吸収体の製造方法。
【選択図】図1
An object of the present invention is to provide a method and an apparatus for manufacturing an absorbent body that can be uniformly dispersed in a water-absorbing polymer in a direction (CD) perpendicular to the flow direction (MD) during production of the absorbent body.
In the method for producing an absorbent body of the present invention, a water-absorbing polymer 51 is introduced into a flow of air flowing in a duct 3 via a polymer supply pipe 5 and is carried on the air flow. Is a method of manufacturing an absorbent body comprising a step of depositing the polymer in a predetermined shape, and the water-absorbing polymer 51 in the polymer supply pipe 5 is accelerated by jetting compressed air, and the accelerated water-absorbing polymer is supplied to the polymer. A method for producing an absorbent body, wherein a water-absorbing polymer dispersed by collision is introduced into the air flow by colliding with a dispersion plate 53 provided on the tip of the tube 5 or an extension line of the polymer supply tube 5.
[Selection] Figure 1

Description

本発明は、吸収体の製造方法及び製造装置に関する。   The present invention relates to an absorbent body manufacturing method and manufacturing apparatus.

生理用ナプキンやパンティライナー、使い捨ておむつ等の吸収性物品の吸収体としては、パルプ繊維等の繊維材料に加えて吸水性ポリマーを含むものが汎用されている。
吸水性ポリマーを含む吸収体の製造においては、吸水性ポリマーを、吸収体製造時の流れ方向(MD)に直交する方向(CD,以下「吸収体の幅方向」ともいう)に均一に分散させることが求められることが多い。
As absorbent bodies for absorbent articles such as sanitary napkins, panty liners, and disposable diapers, those containing water-absorbing polymers in addition to fiber materials such as pulp fibers are widely used.
In the production of an absorbent body containing a water-absorbing polymer, the water-absorbing polymer is uniformly dispersed in a direction perpendicular to the flow direction (MD) at the time of producing the absorbent body (CD, hereinafter also referred to as “absorber width direction”). Is often required.

吸水性ポリマーを、吸収体の幅方向に分散させる技術としては、先端が広がったタイプの供給管を用いる方法や、複数の供給管を並列に並べる方法(共に特許文献1参照)が知られている。   Known techniques for dispersing the water-absorbing polymer in the width direction of the absorbent body include a method using a supply pipe with a widened tip, and a method of arranging a plurality of supply pipes in parallel (both refer to Patent Document 1). Yes.

特開2006−115999号公報JP 2006-115999 A

しかし、先端が広がったタイプの供給管を用いても、吸水性ポリマーが供給管内に充分に分散しない場合が多い。また、複数の供給管を並列に並べる方法は、吸水性ポリマーの散布密度の高い部分が供給管の本数分形成されてしまい均一な分散状態を得ることはできない。   However, even when a supply pipe having a wide tip is used, the water-absorbing polymer is often not sufficiently dispersed in the supply pipe. Moreover, the method of arranging a plurality of supply pipes in parallel cannot form a uniform dispersed state because a portion having a high spray density of the water-absorbing polymer is formed by the number of supply pipes.

従って、本発明の目的は、吸収体製造時の流れ方向(MD)に直交する方向(CD)に吸水性ポリマーを均一に分散させることができる、吸収体の製造方法及び製造装置を提供することにある。   Accordingly, an object of the present invention is to provide an absorbent body manufacturing method and manufacturing apparatus that can uniformly disperse a water-absorbing polymer in a direction (CD) perpendicular to the flow direction (MD) during manufacture of the absorbent body. It is in.

本発明は、ダクト内を流れる空気流中にポリマー供給管を介して吸水性ポリマーを導入し、該空気流に載せて搬送した吸水性ポリマーを所定形状に堆積させる工程を具備する吸収体の製造方法であって、圧縮空気の噴射により、前記ポリマー供給管中の吸水性ポリマーを加速し、加速した該吸水性ポリマーを、該ポリマー供給管の先端部又は該ポリマー供給管の延長線上に設けた分散プレートに衝突させ、衝突により分散した吸水性ポリマーを、前記空気流中に導入する、吸収体の製造方法を提供することにより前記目的を達成したものである。   The present invention provides an absorbent body comprising a step of introducing a water-absorbing polymer into an air flow flowing in a duct via a polymer supply pipe and depositing the water-absorbing polymer carried on the air flow in a predetermined shape. In the method, the water-absorbing polymer in the polymer supply pipe is accelerated by jetting compressed air, and the accelerated water-absorbing polymer is provided on a distal end portion of the polymer supply pipe or an extension line of the polymer supply pipe. The object is achieved by providing a method for producing an absorbent body, in which a water-absorbing polymer that collides with a dispersion plate and is dispersed by the collision is introduced into the air flow.

本発明は、外周面に堆積部を有する回転ドラムと、該回転ドラムの外周面に、内部に生じた空気流に載せて繊維材料及び吸水性ポリマーを供給するダクトとを備えた吸収体の製造装置であって、前記ダクトに、前記吸水性ポリマーを該ダクト内に導入するためのポリマー供給管が設けられ、該ポリマー供給管は、該ポリマー供給管の内部に圧縮空気を噴射する圧縮空気噴射口を有しており、前記ポリマー供給管の先端部又は該ポリマー供給管の延長線上に、前記圧縮空気により加速された吸水性ポリマーを衝突させる分散プレートを有する、吸収体の製造装置を提供することにより前記目的を達成したものである。   The present invention provides an absorbent body comprising a rotating drum having a deposition portion on an outer peripheral surface, and a duct for supplying a fiber material and a water-absorbing polymer on the outer peripheral surface of the rotating drum on an air flow generated inside. An apparatus, wherein the duct is provided with a polymer supply pipe for introducing the water-absorbing polymer into the duct, and the polymer supply pipe is configured to inject compressed air into the polymer supply pipe. Provided is an absorbent manufacturing apparatus having a mouth, and having a dispersion plate that impinges the water-absorbing polymer accelerated by the compressed air on the tip of the polymer supply pipe or an extension of the polymer supply pipe Thus, the object is achieved.

本発明の吸収体の製造方法及び製造装置によれば、吸収体製造時の流れ方向(MD)に直交する方向(CD)に吸水性ポリマーに均一に分散させることができる。   According to the manufacturing method and manufacturing apparatus of the absorbent body of the present invention, it is possible to uniformly disperse the water-absorbing polymer in the direction (CD) orthogonal to the flow direction (MD) during the manufacture of the absorbent body.

以下、本発明をその好ましい実施形態に基づいて説明する。
本発明の一実施形態である吸収体の製造装置1は、図1に示すように、外周面に複数の集積用凹部21(堆積部)が所定の間隔で形成された回転ドラム2と、回転ドラム2の外周面の一部を覆う一端部を有するダクト3を備えている。ダクト3は、回転ドラム2の外周面に、内部に生じた空気流に載せて、繊維材料42及び吸水性ポリマー51を飛散状態にて供給する。
Hereinafter, the present invention will be described based on preferred embodiments thereof.
As shown in FIG. 1, an absorbent body manufacturing apparatus 1 according to an embodiment of the present invention includes a rotary drum 2 having a plurality of accumulation recesses 21 (deposition portions) formed at predetermined intervals on an outer peripheral surface, and a rotating drum 2. A duct 3 having one end portion covering a part of the outer peripheral surface of the drum 2 is provided. The duct 3 supplies the fiber material 42 and the water-absorbing polymer 51 in a scattered state on the outer peripheral surface of the rotating drum 2 while being placed on the air flow generated inside.

回転ドラム2は、円筒状をなし、図1中の矢印A方向に回転駆動されるようになされている。回転ドラム2の外周面には、繊維材料及び吸水性ポリマーの堆積物に付与すべき形状に対応する形状の集積用凹部21,21・・が形成されている。回転ドラム2には、吸気ファン(図示せず)が接続されており、該吸気ファンの駆動により、回転ドラム内の仕切られた空間B及びCを負圧に維持可能に構成されている。個々の集積用凹部21の底面部は、多数の細孔(図示せず)が形成されており、個々の集積用凹部21が、負圧に維持された空間B,C上を通過している間、各集積用凹部21の底面部の細孔が吸引孔として機能する。   The rotating drum 2 has a cylindrical shape and is driven to rotate in the direction of arrow A in FIG. On the outer peripheral surface of the rotating drum 2, accumulation concave portions 21, 21,... Having a shape corresponding to the shape to be imparted to the fibrous material and the water-absorbing polymer deposit are formed. The rotary drum 2 is connected to an intake fan (not shown), and is configured such that the partitioned spaces B and C in the rotary drum can be maintained at a negative pressure by driving the intake fan. A large number of pores (not shown) are formed in the bottom surface of each collecting recess 21, and each collecting recess 21 passes over the spaces B and C maintained at negative pressure. Meanwhile, the pores at the bottom of each accumulation recess 21 function as suction holes.

また、空間B上に位置する集積用凹部21の底面部からの吸引が行われることにより、ダクト3内に、回転ドラム2の外周面に向けて流れる空気流が生じる。
ダクト3における、回転ドラム2側とは反対側の端部付近には、パルプシート等のシート状の吸収体原料41を粉砕して、繊維材料42としてダクト3内に供給する繊維材料供給装置4が設けられている。繊維材料42は、前記吸気ファンの駆動によりダクト内に生じた空気流に随伴して、回転ドラム2の外周面に向けて搬送される。図1中、符号43は、粉砕機である。
In addition, suction from the bottom surface of the accumulation recess 21 located on the space B causes an air flow that flows toward the outer peripheral surface of the rotary drum 2 in the duct 3.
In the vicinity of the end of the duct 3 opposite to the rotating drum 2 side, a fiber material supply device 4 that pulverizes a sheet-like absorbent material 41 such as a pulp sheet and supplies it as a fiber material 42 into the duct 3. Is provided. The fiber material 42 is conveyed toward the outer peripheral surface of the rotating drum 2 along with the air flow generated in the duct by the driving of the intake fan. In FIG. 1, the code | symbol 43 is a grinder.

ダクト3は、上壁31、下壁32及び左右の側壁(図示せず)を有する断面矩形の筒状をなしており、ダクト3における回転ドラム2と繊維材料42の導入部位44との間の上壁31に、吸水性ポリマー51をダクト3内に導入するためのポリマー供給管5が設けられている。
ポリマー供給管5は、図2及び図3に示すように、ポリマー供給管5の内部に圧縮空気を噴射する圧縮空気噴射口52と、圧縮空気により加速された吸水性ポリマー51を衝突させる分散プレート53と、該分散プレート53に衝突した後の吸水性ポリマー51を、ダクト3内に導入するポリマー導入口54とを有している。
The duct 3 has a cylindrical shape with a rectangular cross section having an upper wall 31, a lower wall 32, and left and right side walls (not shown), and between the rotating drum 2 and the introduction portion 44 of the fiber material 42 in the duct 3. A polymer supply pipe 5 for introducing the water-absorbing polymer 51 into the duct 3 is provided on the upper wall 31.
As shown in FIGS. 2 and 3, the polymer supply pipe 5 is a dispersion plate that collides a compressed air injection port 52 that injects compressed air into the polymer supply pipe 5 and a water-absorbing polymer 51 accelerated by the compressed air. 53 and a polymer inlet 54 for introducing the water-absorbing polymer 51 after colliding with the dispersion plate 53 into the duct 3.

図2に示すように、ポリマー供給管5は、断面円形の筒状本体50を主体として構成されており、筒状本体50の内周面に噴射ノズル55の噴射口(圧縮空気噴射口)52が開口している。ポリマー供給管の断面は、ポリマー粉体の流れに対するよどみをつくらないために円形であることが好ましい。噴射ノズル55は、接続管56を介して、電磁弁を備えた圧縮空気のタンク(図示せず)に接続されている。そして、その電磁弁の開閉の制御により、圧縮空気の噴射を制御可能である。圧縮空気のタンクには、コンプレッサーが接続されており、タンク内の圧力が、常時、所定の範囲の圧力に維持されるようになされている。分散プレート53は、筒状本体50を斜めに切断して生じた端部の形状と一致する楕円形状を有している。分散プレート53は、筒状本体50の先端部に固定されている。分散プレート53は、筒状本体50の中心軸線Lに対して傾斜させて設けられており、また、ダクト3の上壁31に対して略平行に設けられている。ポリマー導入口54は、筒状本体50の先端部近傍に切欠部を設けて形成されている。   As shown in FIG. 2, the polymer supply pipe 5 is mainly composed of a cylindrical main body 50 having a circular cross section, and an injection port (compressed air injection port) 52 of the injection nozzle 55 is formed on the inner peripheral surface of the cylindrical main body 50. Is open. The cross section of the polymer supply pipe is preferably circular so as not to cause stagnation with respect to the flow of the polymer powder. The injection nozzle 55 is connected through a connecting pipe 56 to a compressed air tank (not shown) provided with a solenoid valve. The injection of compressed air can be controlled by controlling the opening and closing of the solenoid valve. A compressor is connected to the compressed air tank so that the pressure in the tank is always maintained within a predetermined range. The dispersion plate 53 has an elliptical shape that matches the shape of the end portion produced by cutting the cylindrical body 50 obliquely. The dispersion plate 53 is fixed to the distal end portion of the cylindrical main body 50. The dispersion plate 53 is provided so as to be inclined with respect to the central axis L of the cylindrical main body 50, and is provided substantially parallel to the upper wall 31 of the duct 3. The polymer inlet 54 is formed by providing a notch in the vicinity of the tip of the cylindrical main body 50.

ポリマー供給管5の口径は10〜100mmが好ましく、圧縮空気噴射口52の口径は3〜30mmが好ましく、圧縮空気の供給圧力は圧縮空気噴射口の口径にもよるが、0.02〜1.5MPaであることが好ましい。 The diameter of the polymer supply pipe 5 is preferably 10 to 100 mm, the diameter of the compressed air injection port 52 is preferably 3 to 30 mm, and the supply pressure of the compressed air depends on the diameter of the compressed air injection port. 5 MPa is preferred.

ポリマー供給管5内への圧縮空気の噴射角度θ1(本実施形態においては、噴射ノズル55の中心線の延長線L1と筒状本体50の中心軸線Lとの交差角度,図2参照)は、吸水性ポリマーの効率的な加速の点から、10〜75度、特に20〜50度であることが好ましい。また、噴射ノズル55の中心線の延長線L1上には、開口部54が存在しないことが好ましい。
また、ポリマー供給管5の中心軸線Lと分散プレート53とがなす角度θ2(本実施形態においては、筒状本体50の中心軸線Lと分散プレート53とがなす角度,図2参照)は、吸水性ポリマーの分散性向上の点から、100〜170度、特に110〜50度であることが好ましい。
The injection angle θ1 of compressed air into the polymer supply pipe 5 (in this embodiment, the intersection angle between the extension line L1 of the center line of the injection nozzle 55 and the center axis L of the cylindrical body 50, see FIG. 2) From the viewpoint of efficient acceleration of the water-absorbing polymer, it is preferably 10 to 75 degrees, particularly preferably 20 to 50 degrees. Moreover, it is preferable that the opening 54 does not exist on the extension line L1 of the center line of the injection nozzle 55.
Further, the angle θ2 formed by the central axis L of the polymer supply pipe 5 and the dispersion plate 53 (in this embodiment, the angle formed by the central axis L of the cylindrical main body 50 and the dispersion plate 53, see FIG. 2) is the water absorption. From the viewpoint of improving the dispersibility of the conductive polymer, it is preferably 100 to 170 degrees, particularly preferably 110 to 50 degrees.

本実施形態における分散プレート53は、ポリマー供給管5に直接固定されて設けられているが、これに代えて、分散プレート53を、ダクト3の上壁や左右の側壁等から延びる支持体等(図示せず)に支持させた状態で、ポリマー供給管5の先端部に設けることもできる。
また、図5に示すように、分散プレート53を、ポリマー供給管5の先端部から離間させ、該ポリマー供給管5の延長線上に設けることもできる。この場合、分散プレート53は、例えば、ダクト3の上壁31や左右の側壁等から延びる支持体等(図示せず)に支持させることができる。
分散プレート53の配置位置は、圧縮空気の供給量にもよるが、ダクト3の上壁31からの距離h(図2及び図5参照)が、5〜30cm、特に5〜20cmであることが好ましい。
また、分散プレート53とポリマー供給管5とが分離している場合、分散プレート53とポリマー供給管5の距離L3(図5参照。ポリマー供給管筒状本体50の中心軸線Lに沿って測定)は、ポリマー供給管筒状本体の断面が円形の場合はその径、ポリマー供給管筒状本体の断面が非円形の場合は同面積の円形の径Rとの比R/L3がゼロ(供給管と分散プレートが接触)〜1となる距離が好ましい。
また、ポリマー導入口54は、筒状本体50の中心軸線Lと分散プレート53との交点を中心Pとする左右の開き角度θ3(図3参照)が、100〜360度、特に150〜180度であることが好ましい。
The dispersion plate 53 in the present embodiment is provided directly fixed to the polymer supply pipe 5, but instead of this, the dispersion plate 53 is supported by a support extending from the upper wall, left and right side walls, etc. of the duct 3 ( It can also be provided at the tip of the polymer supply pipe 5 in a state where it is supported by (not shown).
In addition, as shown in FIG. 5, the dispersion plate 53 can be provided on the extension line of the polymer supply pipe 5 while being separated from the tip of the polymer supply pipe 5. In this case, the dispersion plate 53 can be supported by, for example, a support body (not shown) extending from the upper wall 31 and the left and right side walls of the duct 3.
The disposition position of the dispersion plate 53 depends on the supply amount of compressed air, but the distance h (see FIGS. 2 and 5) from the upper wall 31 of the duct 3 is 5 to 30 cm, particularly 5 to 20 cm. preferable.
When the dispersion plate 53 and the polymer supply pipe 5 are separated, the distance L3 between the dispersion plate 53 and the polymer supply pipe 5 (see FIG. 5, measured along the central axis L of the polymer supply pipe cylindrical main body 50). If the cross section of the polymer supply tube cylindrical body is circular, the ratio R / L3 to the circular diameter R of the same area is zero when the cross section of the polymer supply tube cylindrical body is non-circular (supply pipe) And a distance where the dispersion plate is in contact) to 1 is preferable.
The polymer inlet 54 has a left-right opening angle θ3 (see FIG. 3) of 100 to 360 degrees, particularly 150 to 180 degrees, with the intersection point between the center axis L of the cylindrical body 50 and the dispersion plate 53 as the center P. It is preferable that

ポリマー供給管5の筒状本体50のもう一方の端部には、ロート状のポリマー導入管57が接続されており、該ポリマー導入管57の逆円錐状のポリマー投入口58に、図示しないスクリューフィーダー等により吸水性ポリマーが投入され、投入された吸水性ポリマーが、ポリマー導入管57及びポリマー供給管5の筒状本体50を通って、ダクト3内へ供給されるようになされている。   A funnel-shaped polymer introduction pipe 57 is connected to the other end of the cylindrical main body 50 of the polymer supply pipe 5, and a screw (not shown) is connected to an inverted conical polymer inlet 58 of the polymer introduction pipe 57. A water-absorbing polymer is introduced by a feeder or the like, and the introduced water-absorbing polymer is supplied into the duct 3 through the polymer introduction pipe 57 and the cylindrical main body 50 of the polymer supply pipe 5.

ダクト内に供給する繊維材料としては、従来、生理用ナプキンやパンティライナー、使い捨ておむつ等の吸収性物品の吸収体に用いられている各種のものを特に制限なく用いることができる。例えば、パルプ繊維、レーヨン繊維、コットン繊維等のセルロース系繊維の短繊維や、ポリエチレン等の合成繊維の短繊維等が用いられる。これらの繊維は、1種を単独で又は2種以上を組み合わせて用いることができる。
繊維材料は、全体又は一部がパルプ繊維であることが好ましく、繊維材料中のパルプ繊維の割合は20〜100質量%であることが好ましく、より好ましくは80〜100質量%であり、更に好ましくは100質量%である。
As the fiber material supplied into the duct, various materials conventionally used for absorbent bodies of absorbent articles such as sanitary napkins, panty liners, and disposable diapers can be used without particular limitation. For example, short fibers of cellulosic fibers such as pulp fibers, rayon fibers, and cotton fibers, and short fibers of synthetic fibers such as polyethylene are used. These fibers can be used alone or in combination of two or more.
The fiber material is preferably all or part of pulp fiber, and the ratio of pulp fiber in the fiber material is preferably 20 to 100% by mass, more preferably 80 to 100% by mass, and still more preferably. Is 100% by mass.

吸水性ポリマーとしては、従来、使い捨ておむつや生理用ナプキン等の吸収性物品の吸収体に用いられている各種のものを特に制限なく用いることができる。例えば、デンプン系、セルロース系、合成ポリマー系のもの等を用いることができる。吸水性ポリマーは、通常、粒子状である。吸水性ポリマーとしては、自重の20倍以上の液吸収性保持力を有し且つゲル化する性質を有するものが好ましく、例えば、デンプン−アクリル酸(塩)グラフト共重合体、デンプン−アクリロニトリル共重合体のケン化物、ナトリウムカルボキシメチルセルロースの架橋物、アクリル酸(塩)重合体などが好ましい。これらの吸水性ポリマーは、1種を単独で又は2種以上を組み合わせて用いることができる。   As the water-absorbing polymer, various polymers conventionally used for absorbent bodies of absorbent articles such as disposable diapers and sanitary napkins can be used without particular limitation. For example, starch-based, cellulose-based or synthetic polymer-based materials can be used. The water-absorbing polymer is usually in the form of particles. As the water-absorbing polymer, those having a liquid absorbency retention of 20 times or more of its own weight and a gelling property are preferable. For example, starch-acrylic acid (salt) graft copolymer, starch-acrylonitrile copolymer Preferred are a saponified compound, a crosslinked product of sodium carboxymethyl cellulose, an acrylic acid (salt) polymer, and the like. These water-absorbing polymers can be used alone or in combination of two or more.

本実施形態の製造装置1は、図1に示すように、ダクト3内を流れる空気流に載せて飛散状態として搬送した、繊維材料42及び吸水性ポリマー51を、空間B上に位置する集積用凹部21の底面部からの吸引により該集積用凹部21内に堆積させた後、それらの堆積物8を、集積用凹部21内に吸引保持したまま、回転ドラム2の下端部まで搬送し、回転ドラム2の下端部において、堆積物8をバキュームコンベア6上の第1コアラップシート7A上に離型するように構成されている。バキュームコンベア6は、通気性の無端ベルト61及びバキュームボックス62を備えており、無端ベルト61上に、第1コアラップシート7Aが供給された後、第1コアラップシート7A上に、繊維材料及び吸水性ポリマーの堆積物8が載置され、その堆積物8上に、更に第2コアラップシート7Bが供給されるように構成されている。
尚、集積用凹部21からの離型は、回転ドラム2内の仕切られた空間Dを加圧手段(図示せず)により陽圧に維持して、集積用凹部21の底面部の細孔から空気を吹き出させると共に、バキュームコンベア6から吸引することにより行われる。
As shown in FIG. 1, the manufacturing apparatus 1 according to the present embodiment includes a fiber material 42 and a water-absorbing polymer 51 that are transported in an airflow flowing in a duct 3 in a scattered state, and are used for accumulation located in a space B. After being accumulated in the accumulation recess 21 by suction from the bottom surface of the recess 21, the deposit 8 is conveyed to the lower end of the rotary drum 2 while being held in the accumulation recess 21 and rotated. At the lower end of the drum 2, the deposit 8 is configured to be released onto the first core wrap sheet 7 </ b> A on the vacuum conveyor 6. The vacuum conveyor 6 includes a breathable endless belt 61 and a vacuum box 62. After the first core wrap sheet 7A is supplied onto the endless belt 61, the fiber material and A deposit 8 of a water-absorbing polymer is placed, and the second core wrap sheet 7B is further supplied onto the deposit 8.
The mold release from the recess 21 for accumulation is performed by maintaining the space D partitioned in the rotary drum 2 at a positive pressure by a pressurizing means (not shown) and from the pores at the bottom of the recess 21 for accumulation. Air is blown out and sucked from the vacuum conveyor 6.

上述した吸収体の製造装置1を用いた吸収体の製造方法、即ち本発明の吸収体の製造方法の一実施形態について説明する。
本実施形態の吸収体の製造方法は、ダクト3内を流れる空気流中にポリマー供給管5を介して吸水性ポリマー51を導入し、該空気流に載せて搬送した吸水性ポリマー51を所定形状に堆積させる工程を具備しており、当該工程において、圧縮空気の噴射により、前記ポリマー供給管5中の吸水性ポリマーを51加速し、加速した吸水性ポリマー51を、該ポリマー供給管5の先端部に設けた分散プレート53に衝突させた後、ダクト3内に導入する。
本実施形態においては、ポリマー供給管5中に圧縮空気を噴射し、ポリマー供給管5中の吸水性ポリマー51を加速している。
An embodiment of an absorber manufacturing method using the absorber manufacturing apparatus 1 described above, that is, an embodiment of the absorber manufacturing method of the present invention will be described.
In the manufacturing method of the absorbent body according to the present embodiment, the water-absorbing polymer 51 is introduced into the air flow flowing in the duct 3 through the polymer supply pipe 5, and the water-absorbing polymer 51 conveyed on the air flow is shaped into a predetermined shape. In which the water-absorbing polymer 51 in the polymer supply pipe 5 is accelerated by jetting compressed air, and the accelerated water-absorbing polymer 51 is added to the tip of the polymer supply pipe 5. After colliding with the dispersion plate 53 provided in the section, it is introduced into the duct 3.
In the present embodiment, compressed air is injected into the polymer supply pipe 5 to accelerate the water-absorbing polymer 51 in the polymer supply pipe 5.

本実施形態の製造方法について更に詳細に説明する。
吸収体の製造装置1を用いて吸収体を製造するためには、回転ドラム2を回転させると共に、上記吸気ファンを作動させて空間B及びCを負圧にする。また、バキュームコンベア6を作動させ、更に第1及び第2コアラップシート7A,7Bの供給機構も作動させる。
吸気ファンの作動により、空間B上に位置する集積用凹部20の底面部に吸引力が生じると共に、ダクト3内に、回転ドラム2の外周面に向けて流れる空気流が生じる。
The manufacturing method of this embodiment will be described in further detail.
In order to manufacture the absorber using the absorber manufacturing apparatus 1, the rotary drum 2 is rotated and the intake fan is operated to make the spaces B and C have a negative pressure. Further, the vacuum conveyor 6 is operated, and the supply mechanism for the first and second core wrap sheets 7A and 7B is also operated.
By the operation of the intake fan, a suction force is generated on the bottom surface portion of the accumulation recess 20 located on the space B, and an air flow that flows toward the outer peripheral surface of the rotary drum 2 is generated in the duct 3.

そして、繊維材料供給装置4を作動させて、ダクト3内に繊維材料42を供給すると、該繊維材料42は、飛散状態となって、ダクト3内を流れる空気流に載って搬送され、回転ドラム2の外周面に向けて供給される。   When the fiber material supply device 4 is operated to supply the fiber material 42 into the duct 3, the fiber material 42 is in a scattered state and is carried on the air flow flowing through the duct 3, and the rotating drum. 2 is supplied toward the outer peripheral surface.

また、スクリューフィーダー等を作動させ、吸水性ポリマーをポリマー投入口58に投入し、また、圧縮空気噴射口52から圧縮空気を噴射させる。
ポリマー投入口58に投入された吸水性ポリマーは、主としてダクトに生じた空気流の影響によりポリマー導入管57及びポリマー供給管5内に生じる空気の流れと、自重によって、ポリマー供給管5内へと導かれる。
そして、ポリマー供給管5中の吸水性ポリマーに対して、圧縮空気噴射口52から圧縮空気が噴射され、吸水性ポリマーは、移動速度が急激に上昇し、高い運動エネルギーを持って分散プレート53に衝突する。そして、衝突した吸水性ポリマーは、分散プレートに跳ね返されて多様な方向に飛び散り、飛び散った吸水性ポリマーが、ポリマー導入口54からダクト3内へと導入される。
Further, the screw feeder or the like is operated, the water-absorbing polymer is introduced into the polymer inlet 58, and the compressed air is injected from the compressed air outlet 52.
The water-absorbing polymer introduced into the polymer introduction port 58 flows into the polymer supply pipe 5 by the air flow generated in the polymer introduction pipe 57 and the polymer supply pipe 5 mainly by the influence of the air flow generated in the duct and by its own weight. Led.
Then, compressed air is injected from the compressed air injection port 52 to the water-absorbing polymer in the polymer supply pipe 5, and the moving speed of the water-absorbing polymer rapidly increases, and has a high kinetic energy to the dispersion plate 53. collide. Then, the collided water-absorbing polymer is bounced back to the dispersion plate and scattered in various directions, and the scattered water-absorbing polymer is introduced into the duct 3 from the polymer inlet 54.

このように、圧縮空気の噴射により加速させた吸水性ポリマーを分散プレートに衝突させた後、ダクト内に導入することにより、吸水性ポリマー51は、図4(a)に示すように、ダクト3内の幅方向(Y方向)に広く分散した状態となり、その分散状態を維持した状態で、繊維材料42と共に、集積用凹部21に堆積する。尚、図4(b)は、圧縮空気を噴射しない以外は同様にして、吸水性ポリマー51をダクト3内に導入した場合の吸水性ポリマー51の分散状態を示したものである。   In this way, the water-absorbing polymer 51 accelerated by the jet of compressed air collides with the dispersion plate and then introduced into the duct, so that the water-absorbing polymer 51 has the duct 3 as shown in FIG. It is in a state of being widely dispersed in the inner width direction (Y direction), and is deposited in the accumulation concave portion 21 together with the fiber material 42 while maintaining the dispersed state. FIG. 4B shows the dispersion state of the water-absorbing polymer 51 when the water-absorbing polymer 51 is introduced into the duct 3 in the same manner except that the compressed air is not injected.

集積用凹部21内の繊維材料21及び吸水性ポリマー51の堆積物8は、回転ドラム2の下端部まで搬送され、集積用凹部21の形状に対応する形状に成形された堆積物8として、集積用凹部21から離型される。
そして、集積用凹部21から離型された堆積物8は、第1及び第2コアラップシート7A,7B間に配置されて、吸収体の連続体9とされる。この吸収体の連続体9は、公知の搬送手段により後の工程に搬送され、公知の切断手段により切断されて、個々の吸収性物品に使用される吸収体9となる。
The deposit 8 of the fiber material 21 and the water-absorbing polymer 51 in the accumulation recess 21 is conveyed to the lower end of the rotary drum 2 and accumulated as a deposit 8 formed into a shape corresponding to the shape of the accumulation recess 21. The mold is released from the recess 21 for use.
Then, the deposit 8 released from the accumulation recess 21 is disposed between the first and second core wrap sheets 7A and 7B to form a continuous body 9 of the absorber. The continuous body 9 of the absorbent body is transported to a subsequent process by a known transporting means, and is cut by a known cutting means to become an absorbent body 9 used for each absorbent article.

本実施形態の製造装置及び製造方法によれば、上述のように、吸水性ポリマーを圧縮空気の噴射により加速させ分散プレートに衝突させた後、ダクト内に導入することにより、吸水性ポリマーをダクト3内の幅方向(Y方向)に幅広く且つ均一に分散させることができ、それにより、吸収体製造時の流れ方向(MD)に直交する方向に均一に分散した吸収体9を効率的に製造することができる。   According to the manufacturing apparatus and the manufacturing method of the present embodiment, as described above, the water-absorbing polymer is accelerated by jetting compressed air, collides with the dispersion plate, and then introduced into the duct, whereby the water-absorbing polymer is ducted. 3 can be dispersed widely and uniformly in the width direction (Y direction), and thereby efficiently produce the absorbent body 9 uniformly dispersed in the direction perpendicular to the flow direction (MD) during the production of the absorbent body. can do.

以上、本発明の吸収体の製造方法及び製造装置それぞれの一実施形態について説明したが、本発明は、上記各実施形態に制限されず適宜変更可能である。
例えば、上述した実施形態においては、集積用凹部21から離型させた、繊維材料及び吸水性ポリマーの堆積物8の上下面を、第1及び第2コアラップシート7A,7Bで被覆したが、これに代えて、当該堆積物8の上下面を一枚のコアラップシートで被覆した吸収体を製造しても良く、また、当該堆積物8の上下面の一方又は両方を被覆しない吸収体を製造しても良い。
As mentioned above, although each embodiment of the manufacturing method and manufacturing apparatus of the absorber of this invention was described, this invention is not restrict | limited to said each embodiment, It can change suitably.
For example, in the above-described embodiment, the upper and lower surfaces of the fibrous material and water-absorbing polymer deposit 8 released from the accumulation recess 21 are covered with the first and second core wrap sheets 7A and 7B. Alternatively, an absorber in which the upper and lower surfaces of the deposit 8 are covered with a single core wrap sheet may be manufactured, and an absorber that does not cover one or both of the upper and lower surfaces of the deposit 8 may be manufactured. It may be manufactured.

また、集積用凹部21は、回転ドラム2の外周面に、周方向に連続する溝状の凹部として形成されていても良い。
また、本発明の方法及び装置においては、非凹状の堆積部に、吸水性ポリマーや繊維材料を堆積させても良い。例えば、ダクトに臨む面に凹部が形成されていないメッシュコンベアや外周面に凹部が形成されていない回転ドラムの外周面における一定の領域のみに吸引力を作用させ、該一定領域のみに吸水性ポリマーや繊維材料を堆積させても良い。この場合、その吸引力を作用させる部分が堆積部である。
The accumulation recess 21 may be formed on the outer peripheral surface of the rotary drum 2 as a groove-like recess that is continuous in the circumferential direction.
In the method and apparatus of the present invention, a water-absorbing polymer or a fiber material may be deposited on the non-concave deposition portion. For example, a suction force is applied only to a certain region on the outer peripheral surface of a mesh conveyor having no concave portion formed on the surface facing the duct or a concave portion formed on the outer peripheral surface, and the water absorbent polymer is applied only to the predetermined region. Or a fiber material may be deposited. In this case, the portion where the suction force is applied is the deposition portion.

また、ポリマー供給管5は、断面円形の筒状本体50に代えて、中心軸線Lに直交する断面形状が非円形の筒状本体を備えたものであっても良い。例えば、中心軸線に直交する断面形状が、楕円形、正方形、長方形、台形、菱形、三角形等の筒状本体を備えたものを用いることもできる。また、圧縮空気の噴射口52が、筒状本体50の内部に突き出した状態に設けることもできる。分散プレート53の形状も、楕円形以外の形状とすることもできる。また、噴射ノズル55は、ポリマー導入管57の逆円錐台状部分以外の部分に設けることもできる。   The polymer supply pipe 5 may be provided with a cylindrical main body having a non-circular cross section perpendicular to the central axis L instead of the cylindrical main body 50 having a circular cross section. For example, a cross-sectional shape perpendicular to the central axis may include an oval, square, rectangular, trapezoidal, rhombus, triangular, or other cylindrical body. Further, the compressed air injection port 52 can be provided in a state of protruding into the cylindrical main body 50. The shape of the dispersion plate 53 can also be a shape other than an ellipse. The injection nozzle 55 can also be provided in a portion other than the inverted truncated cone portion of the polymer introduction tube 57.

また、図6に示すように、ポリマー供給管5に、吸水性ポリマー51の流路50aに連通するが内部をポリマーが通らない分岐部分59を設け、該分岐部分59に設けた圧縮空気の噴射口52から噴射した圧縮空気により、該噴射口52より下流(ポリマー導入口54側)の位置から供給される吸水性ポリマー51を加速しても良い。この場合、図中には示していないが吸水性ポリマー51を圧縮空気の圧力に抗して導入するため、ポリマー押し出し手段と弁とを備えた装置等を備えている。   In addition, as shown in FIG. 6, the polymer supply pipe 5 is provided with a branch portion 59 that communicates with the flow path 50 a of the water-absorbing polymer 51 but does not allow the polymer to pass therethrough, and jets of compressed air provided in the branch portion 59 The water-absorbing polymer 51 supplied from a position downstream of the injection port 52 (on the polymer introduction port 54 side) may be accelerated by the compressed air injected from the port 52. In this case, although not shown in the figure, in order to introduce the water-absorbing polymer 51 against the pressure of the compressed air, a device including a polymer pushing means and a valve is provided.

また、吸水性ポリマーを、繊維材料を搬送する空気流中に導入し、混合状態とされた該繊維材料及び該吸水性ポリマーを、集積用凹部(堆積部)に堆積させるのに代えて、集積用凹部(堆積部)に繊維材料を堆積させ、その後、堆積した繊維材料の上に、繊維材料を含まない空気流によって搬送した吸水性ポリマーを堆積させても良い。   In addition, instead of depositing the water-absorbing polymer into the air flow that conveys the fiber material and depositing the mixed fiber material and the water-absorbing polymer in the concave portion for accumulation (deposition portion), accumulation is performed. The fiber material may be deposited in the concave portion (deposition portion), and then the water-absorbing polymer conveyed by the air flow not containing the fiber material may be deposited on the deposited fiber material.

本発明の吸収体の製造装置の一実施形態を示す模式図である。It is a schematic diagram which shows one Embodiment of the manufacturing apparatus of the absorber of this invention. 図1に示す吸収体の製造装置におけるポリマー供給管の詳細を示す図で、図2(a)は、ダクト内の空気流の流れ方向に沿う鉛直断面図、図2(b)は、ポリマー供給管を、空気流の流れ方向の下流側のやや上方から見た斜視図である。It is a figure which shows the detail of the polymer supply pipe | tube in the manufacturing apparatus of the absorber shown in FIG. 1, FIG. 2 (a) is a vertical sectional view along the flow direction of the air flow in a duct, FIG.2 (b) is a polymer supply. It is the perspective view which looked at the pipe | tube from the upper side of the downstream of the flow direction of an airflow. 図1に示す吸収体の製造装置におけるポリマー供給管の先端部付近を、ポリマー導入口側から見た状態を示す斜視図である。It is a perspective view which shows the state which looked at the front-end | tip part vicinity of the polymer supply pipe | tube in the manufacturing apparatus of the absorber shown in FIG. 1 from the polymer inlet side. 本発明の作用効果を示す説明図であり、図4(a)は、圧縮空気を噴射した場合の吸水性ポリマーの分散態様を示し、図4(b)は、圧縮空気を噴射しない場合の吸水性ポリマーの分散態様を示す図である。4A and 4B are explanatory diagrams showing the operational effects of the present invention. FIG. 4A shows a dispersion mode of the water-absorbing polymer when compressed air is injected, and FIG. 4B shows water absorption when compressed air is not injected. It is a figure which shows the dispersion | distribution aspect of a conductive polymer. 本発明の吸収体の製造装置の他の実施形態を示す図(図2相当図)である。It is a figure (figure 2 equivalent figure) which shows other embodiment of the manufacturing apparatus of the absorber of this invention. 本発明の吸収体の製造装置の更に他の実施形態を示す図(図2相当図)である。It is a figure (FIG. 2 equivalent figure) which shows other embodiment of the manufacturing apparatus of the absorber of this invention.

符号の説明Explanation of symbols

1 吸収体の製造装置
2 回転ドラム
21 集積用凹部(堆積部)
3 ダクト
4 繊維材料供給装置
41 シート状の吸収体原料
42 繊維材料
5 ポリマー供給管
51 吸水性ポリマー
52 圧縮空気噴射口
53 分散プレート
54 ポリマー導入口
55 噴射ノズル
56 接続管
57 ポリマー導入管
6 バキュームコンベア
7A,7B 第1及び第2コアラップシート
8 繊維材料及び吸水性ポリマーの堆積物
9 吸収体
9A 吸収体の連続体
DESCRIPTION OF SYMBOLS 1 Absorber manufacturing apparatus 2 Rotating drum 21 Accumulation recess (deposition part)
DESCRIPTION OF SYMBOLS 3 Duct 4 Fiber material supply apparatus 41 Sheet-form absorber raw material 42 Fiber material 5 Polymer supply pipe 51 Water-absorbing polymer 52 Compressed air injection port 53 Dispersion plate 54 Polymer introduction port 55 Injection nozzle 56 Connection pipe 57 Polymer introduction tube 6 Vacuum conveyor 7A, 7B First and second core wrap sheets 8 Deposits of fiber material and water-absorbing polymer 9 Absorber 9A Absorber continuum

Claims (4)

ダクト内を流れる空気流中にポリマー供給管を介して吸水性ポリマーを導入し、該空気流に載せて搬送した吸水性ポリマーを所定形状に堆積させる工程を具備する吸収体の製造方法であって、
圧縮空気の噴射により、前記ポリマー供給管中の吸水性ポリマーを加速し、加速した該吸水性ポリマーを、該ポリマー供給管の先端部又は該ポリマー供給管の延長線上に設けた分散プレートに衝突させ、衝突により分散した吸水性ポリマーを、前記空気流中に導入する、吸収体の製造方法。
A method for producing an absorbent body comprising a step of introducing a water-absorbing polymer into a flow of air flowing in a duct via a polymer supply pipe and depositing the water-absorbing polymer carried on the air flow in a predetermined shape. ,
The water-absorbing polymer in the polymer supply pipe is accelerated by jetting compressed air, and the accelerated water-absorbing polymer is made to collide with a dispersion plate provided on the tip of the polymer supply pipe or an extension line of the polymer supply pipe. A method for producing an absorbent body, wherein a water-absorbing polymer dispersed by collision is introduced into the air stream.
前記ダクトを流れる空気流が繊維材料を含んでいる請求項1記載の吸収体の製造方法。   The manufacturing method of the absorber of Claim 1 in which the airflow which flows through the said duct contains the fiber material. 外周面に堆積部を有する回転ドラムと、該回転ドラムの外周面に、内部に生じた空気流に載せて繊維材料及び吸水性ポリマーを供給するダクトとを備えた吸収体の製造装置であって、
前記ダクトに、前記吸水性ポリマーを該ダクト内に導入するためのポリマー供給管が設けられ、該ポリマー供給管は、該ポリマー供給管の内部に圧縮空気を噴射する圧縮空気噴射口を有しており、
前記ポリマー供給管の先端部又は該ポリマー供給管の延長線上に、前記圧縮空気により加速された吸水性ポリマーを衝突させる分散プレートを有する、吸収体の製造装置。
An apparatus for manufacturing an absorbent body, comprising: a rotating drum having a deposition portion on an outer peripheral surface; and a duct for supplying a fiber material and a water-absorbing polymer on an air flow generated inside the rotating drum on the outer peripheral surface of the rotating drum. ,
The duct is provided with a polymer supply pipe for introducing the water-absorbing polymer into the duct, and the polymer supply pipe has a compressed air injection port for injecting compressed air into the polymer supply pipe. And
The absorber manufacturing apparatus which has a dispersion | distribution plate which collides the water absorbing polymer accelerated with the said compressed air on the front-end | tip part of the said polymer supply pipe, or the extension line of this polymer supply pipe.
前記ポリマー供給管の中心軸線Lと前記分散プレートとのなす角度θ2が、100〜170度である請求項3記載の吸収体の製造装置。   The absorber manufacturing apparatus according to claim 3, wherein an angle θ <b> 2 formed by a central axis L of the polymer supply pipe and the dispersion plate is 100 to 170 degrees.
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