TW202413760A - Long fiber nonwoven fabric and manufacturing method thereof, and laminate, filter, protective clothing, and face mask - Google Patents

Long fiber nonwoven fabric and manufacturing method thereof, and laminate, filter, protective clothing, and face mask Download PDF

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TW202413760A
TW202413760A TW112133772A TW112133772A TW202413760A TW 202413760 A TW202413760 A TW 202413760A TW 112133772 A TW112133772 A TW 112133772A TW 112133772 A TW112133772 A TW 112133772A TW 202413760 A TW202413760 A TW 202413760A
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nonwoven fabric
long
fiber nonwoven
less
organic peroxide
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池田雄太
勝田大士
森岡英樹
梶原健太郎
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日商東麗股份有限公司
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本發明的課題在於提供一種粒子的捕集效率與通氣性此兩者優異的不織布,本發明的主旨為一種長纖維不織布,其包括包含聚丙烯系樹脂的纖維,且所述長纖維不織布中,所述纖維的平均纖維徑為0.05 μm以上且5.00 μm以下,所述長纖維不織布於190℃的零剪切黏度為5 Pa·s以上且10 Pa·s以下。The subject of the present invention is to provide a nonwoven fabric having excellent particle capture efficiency and air permeability. The main purpose of the present invention is a long-fiber nonwoven fabric, which includes fibers containing a polypropylene resin, and in the long-fiber nonwoven fabric, the average fiber diameter of the fibers is greater than 0.05 μm and less than 5.00 μm, and the zero shear viscosity of the long-fiber nonwoven fabric at 190°C is greater than 5 Pa·s and less than 10 Pa·s.

Description

長纖維不織布及其製造方法、以及積層體、過濾器、防護服、面罩Long fiber nonwoven fabric and its manufacturing method, as well as laminate, filter, protective clothing, and mask

本發明是有關於一種長纖維不織布及其製造方法。The present invention relates to a long-fiber nonwoven fabric and a manufacturing method thereof.

近年來,包含聚丙烯系樹脂的纖維或不織布被供於面罩或一次性尿布等衛生材料、防護服、過濾器等各種用途。特別是,關於面罩或防護服、過濾器用途中所使用的不織布,為了提高粒子的捕集效率或液體的阻隔性而對構成纖維要求極細化。In recent years, fibers and nonwoven fabrics containing polypropylene resins have been used in various applications such as sanitary materials such as masks and disposable diapers, protective clothing, filters, etc. In particular, nonwoven fabrics used in masks, protective clothing, and filters are required to have extremely fine constituent fibers in order to improve particle capture efficiency and liquid barrier properties.

例如,於專利文獻1中所揭示的技術中,作為能夠生產性良好地製造包含極細纖維的熔噴不織布的聚丙烯,提出了一種熔體流動速率為一定以上且分子量分佈(Mw/Mn)為一定以下的聚丙烯樹脂。另外,於專利文獻2~專利文獻4中所揭示的技術中,提出了一種將數量平均纖維徑或不織布的細孔徑等設為特定的範圍的不織布。 [現有技術文獻] [專利文獻] For example, in the technology disclosed in Patent Document 1, a polypropylene resin having a melt flow rate of a certain value or more and a molecular weight distribution (Mw/Mn) of a certain value or less is proposed as a polypropylene capable of producing a melt-blown nonwoven fabric containing ultrafine fibers with good productivity. In addition, in the technology disclosed in Patent Documents 2 to 4, a nonwoven fabric is proposed in which the number average fiber diameter or the pore diameter of the nonwoven fabric is set to a specific range. [Prior Art Document] [Patent Document]

專利文獻1:日本專利特開2002-201560號公報 專利文獻2:日本專利特開2016-053241號公報 專利文獻3:國際公開第2012/014501號 專利文獻4:國際公開第2016/148174號 Patent document 1: Japanese Patent Publication No. 2002-201560 Patent document 2: Japanese Patent Publication No. 2016-053241 Patent document 3: International Publication No. 2012/014501 Patent document 4: International Publication No. 2016/148174

[發明所欲解決之課題] 於專利文獻1中所揭示的技術中,存在如下課題:由於使用熔體流動速率相當高的聚丙烯,因此於紡紗步驟中纖維不易固化,為了提高生產效率而進行高速紡紗時,於製成不織布時,來不及進行冷卻而成為緻密的不織布,所獲得的不織布的通氣度有時降低。另外,於專利文獻2中所揭示的技術中,存在如下課題:為了將最大細孔徑、平均細孔徑設為一定值以下而縮短紡紗機與捕集部的距離,因此於捕集部纖維進行熔接時,被熱風強力按壓,藉此空隙率降低,不織布的通氣性降低。進而,於專利文獻3中所揭示的技術中,存在如下課題:為了獲得平均纖維徑更細的纖維而對纖維狀的熔融樹脂進行電壓施加,因此樹脂劣化,會形成強度低的不織布。而且,於專利文獻4中所揭示的技術中,存在如下課題:為了獲得平均纖維徑更細的纖維而使每個紡紗噴嘴的樹脂噴出量極低,因此有噴出不穩定而不織布的均勻性降低的傾向。 [Problems to be solved by the invention] The technology disclosed in patent document 1 has the following problems: Since polypropylene with a high melt flow rate is used, the fibers are not easy to solidify in the spinning step. When high-speed spinning is performed to improve production efficiency, the nonwoven fabric is not cooled in time to form a dense nonwoven fabric, and the air permeability of the obtained nonwoven fabric is sometimes reduced. In addition, the technology disclosed in patent document 2 has the following problems: In order to set the maximum pore size and the average pore size below a certain value, the distance between the spinning machine and the collection part is shortened. Therefore, when the fibers are welded in the collection part, they are strongly pressed by hot air, thereby reducing the porosity and reducing the air permeability of the nonwoven fabric. Furthermore, in the technology disclosed in Patent Document 3, there is the following problem: in order to obtain fibers with a finer average fiber diameter, a voltage is applied to the fibrous molten resin, so the resin deteriorates and a nonwoven fabric with low strength is formed. Moreover, in the technology disclosed in Patent Document 4, there is the following problem: in order to obtain fibers with a finer average fiber diameter, the resin spraying amount of each spinning nozzle is extremely low, so there is a tendency for the spraying to be unstable and the uniformity of the nonwoven fabric to be reduced.

因此,本發明是鑒於所述情況而成,其課題在於提供一種粒子的捕集效率與通氣性此兩者優異的不織布。 [解決課題之手段] Therefore, the present invention is made in view of the above situation, and its subject is to provide a non-woven fabric with excellent particle capture efficiency and air permeability. [Means for solving the problem]

於專利文獻1中記載有:作為特佳的聚丙烯樹脂,較佳為將熔體流動速率(melt flow rate)(以下,有時簡記為「MFR」)為20 g/10分鐘以下的聚丙烯降解(degradation)而獲得者。然而,本發明者等人進行研究,結果可知:此種不織布有於降解的過程中容易切斷聚丙烯中的分子鏈更長者的傾向,因此於紡紗步驟中纖維不易固化,於製成不織布時形成得緻密,通氣性有時降低。因此,進一步重複進行努力研究,結果發現:藉由將構成長纖維不織布的丙烯系樹脂纖維的平均纖維徑及聚丙烯系樹脂的零剪切黏度設為特定的範圍,可獲得粒子的捕集效率與通氣性此兩者優異的不織布。Patent document 1 states that a particularly preferred polypropylene resin is preferably one obtained by degradation of polypropylene having a melt flow rate (hereinafter, sometimes abbreviated as "MFR") of 20 g/10 minutes or less. However, the inventors and others conducted research and found that such nonwoven fabrics tend to easily cut longer molecular chains in the polypropylene during the degradation process, so that the fibers are not easily solidified during the spinning step, and the nonwoven fabrics are formed densely when they are made, and the air permeability is sometimes reduced. Therefore, further repeated efforts have led to the discovery that by setting the average fiber diameter of the acrylic resin fibers that make up the long-fiber nonwoven fabric and the zero shear viscosity of the polypropylene resin to a specific range, a nonwoven fabric with excellent particle capture efficiency and air permeability can be obtained.

本發明是基於該些見解而完成,藉由本發明,可提供以下發明。The present invention is accomplished based on these findings, and the following inventions can be provided by the present invention.

[1] 一種長纖維不織布,包括包含聚丙烯系樹脂的纖維,且所述長纖維不織布中,所述纖維的平均纖維徑為0.05 μm以上且5.00 μm以下,所述長纖維不織布於190℃的零剪切黏度為5 Pa·s以上且10 Pa·s以下。[1] A long fiber nonwoven fabric comprising fibers containing a polypropylene resin, wherein the average fiber diameter of the fibers in the long fiber nonwoven fabric is greater than or equal to 0.05 μm and less than or equal to 5.00 μm, and the zero shear viscosity of the long fiber nonwoven fabric at 190°C is greater than or equal to 5 Pa·s and less than or equal to 10 Pa·s.

[2] 如所述[1]所記載的長纖維不織布,其中,所述長纖維不織布含有100 ppm以上且1000 ppm以下的具有以下的通式(1)或通式(2)所表示的結構的有機過氧化物。[2] The long fiber nonwoven fabric as described in [1], wherein the long fiber nonwoven fabric contains 100 ppm or more and 1000 ppm or less of an organic peroxide having a structure represented by the following general formula (1) or (2).

[化1] [Chemistry 1]

[化2] [Chemistry 2]

此處,R 1~R 3、R 5~R 7為碳原子數1~10的烷基、烯基、苯基、苄基或苯甲醯基,R 4、R 8為碳原子數1~20且除碳原子以外僅包含氫原子的結構。 Here, R 1 to R 3 and R 5 to R 7 are alkyl, alkenyl, phenyl, benzyl or benzoyl groups having 1 to 10 carbon atoms, and R 4 and R 8 are structures having 1 to 20 carbon atoms and containing only hydrogen atoms other than carbon atoms.

[3] 如[1]或[2]所述的長纖維不織布,其中,藉由凝膠滲透層析法而求出的所述聚丙烯系樹脂的分子量分佈Mw/Mn為2.00以上且4.00以下。此處,Mw、Mn分別為聚合平均分子量、數量平均分子量。[3] The long fiber nonwoven fabric according to [1] or [2], wherein the molecular weight distribution Mw/Mn of the polypropylene resin determined by gel permeation chromatography is 2.00 or more and 4.00 or less. Here, Mw and Mn are polymerization average molecular weight and number average molecular weight, respectively.

[4] 如所述[1]或[2]所記載的長纖維不織布,其中,所述長纖維不織布的空隙率為92.5%以上且99.0%以下。[4] The long fiber nonwoven fabric as described in [1] or [2], wherein the porosity of the long fiber nonwoven fabric is greater than or equal to 92.5% and less than or equal to 99.0%.

[5] 一種積層體,具有至少一層包含如所述[1]至[4]中任一項所記載的長纖維不織布的層。[5] A laminate having at least one layer comprising the long-fiber nonwoven fabric as described in any one of [1] to [4].

[6] 一種過濾器,使用如所述[1]至[4]中任一項所記載的長纖維不織布。[6] A filter using the long fiber nonwoven fabric as described in any one of [1] to [4].

[7] 一種防護服,使用如所述[1]至[4]中任一項所記載的長纖維不織布。[7] A protective clothing comprising the long-fiber nonwoven fabric as described in any one of [1] to [4].

[8] 一種面罩,使用如所述[1]至[4]中任一項所記載的長纖維不織布。[8] A face mask comprising the long fiber nonwoven fabric as described in any one of [1] to [4].

[9] 一種長纖維不織布的製造方法,將於溶體流動速率為500 g/10分鐘以上且2000 g/10分鐘以下的聚丙烯系樹脂中添加具有以下的通式(1)或通式(2)所表示的結構的有機過氧化物而得的原料樹脂組成物熔融而獲得熔融樹脂,對該熔融樹脂實施熔噴法而獲得長纖維不織布。[9] A method for producing a long-fiber nonwoven fabric comprises: melting a raw material resin composition obtained by adding an organic peroxide having a structure represented by the following general formula (1) or (2) to a polypropylene resin having a melt flow rate of 500 g/10 min or more and 2000 g/10 min or less to obtain a molten resin; and subjecting the molten resin to a melt spraying method to obtain a long-fiber nonwoven fabric.

[化3] [Chemistry 3]

[化4] [Chemistry 4]

此處,R 1~R 3、R 5~R 7為碳原子數1~10的烷基、烯基、苯基、苄基或苯甲醯基,R 4、R 8為碳原子數1~20且除碳原子以外僅包含氫原子的結構。 Here, R 1 to R 3 and R 5 to R 7 are alkyl, alkenyl, phenyl, benzyl or benzoyl groups having 1 to 10 carbon atoms, and R 4 and R 8 are structures having 1 to 20 carbon atoms and containing only hydrogen atoms other than carbon atoms.

[10] 如[9]所述的長纖維不織布的製造方法,其中,藉由如下方式而獲得所述熔融樹脂:使所述聚丙烯系樹脂與所述有機過氧化物於用以向實施所述熔噴法的紡紗機中供給原料的擠出機內反應。[10] The method for producing a long-fiber nonwoven fabric as described in [9], wherein the molten resin is obtained by reacting the polypropylene-based resin and the organic peroxide in an extruder for supplying raw materials to a spinning machine for performing the melt blowing method.

[11] 如[9]或[10]所述的長纖維不織布的製造方法,其中,將所述有機過氧化物以混練聚丙烯系樹脂與有機過氧化物而得的母料的形態添加。[11] The method for producing a long-fiber nonwoven fabric as described in [9] or [10], wherein the organic peroxide is added in the form of a masterbatch obtained by kneading a polypropylene-based resin and the organic peroxide.

[12] 如所述[9]至[11]中任一項所記載的長纖維不織布的製造方法,其中,所述原料樹脂組成物中的所述有機過氧化物的添加量為0.2質量%以上且1.0質量%以下。 [發明的效果] [12] A method for producing a long fiber nonwoven fabric as described in any one of [9] to [11], wherein the amount of the organic peroxide added to the raw material resin composition is 0.2 mass % or more and 1.0 mass % or less. [Effect of the invention]

藉由本發明,可獲得能效率良好地捕集粒子且通氣性亦優異的適合用作過濾器或面罩、防護服的集塵層或耐水層的長纖維不織布。According to the present invention, a long-fiber nonwoven fabric can be obtained which can efficiently capture particles and has excellent air permeability and is suitable for use as a filter or a dust collecting layer or a water-resistant layer of a mask or protective clothing.

本發明的不織布為包括包含聚丙烯系樹脂的纖維的長纖維不織布,且所述纖維的平均纖維徑為0.05 μm以上且5.00 μm以下,所述長纖維不織布於190℃的零剪切黏度為5 Pa·s以上且10 Pa·s以下。以下,對其結構要素進行詳細說明,但本發明只要不超過其主旨,則並不受以下說明的範圍的任何限定。The nonwoven fabric of the present invention is a long-fiber nonwoven fabric including fibers containing a polypropylene resin, and the average fiber diameter of the fibers is 0.05 μm or more and 5.00 μm or less, and the zero shear viscosity of the long-fiber nonwoven fabric at 190° C. is 5 Pa·s or more and 10 Pa·s or less. The structural elements thereof are described in detail below, but the present invention is not limited to the scope of the following description as long as it does not exceed the gist thereof.

[聚丙烯系樹脂] 本發明的長纖維不織布包含聚丙烯系樹脂。所謂本發明中的「聚丙烯系樹脂」,是指丙烯單元於重複單元中所佔的莫耳分率為80莫耳%~100莫耳%的樹脂。藉由使用聚丙烯系樹脂,從而形成成本低且拉伸強度或加工性優異的不織布。 [Polypropylene resin] The long-fiber nonwoven fabric of the present invention contains a polypropylene resin. The so-called "polypropylene resin" in the present invention refers to a resin in which the molar fraction of propylene units in repeating units is 80 mol% to 100 mol%. By using a polypropylene resin, a nonwoven fabric with low cost and excellent tensile strength or processability can be formed.

本發明中的聚丙烯系樹脂例如可含有丙烯均聚物、丙烯與各種α-烯烴的共聚物等。此處,所謂α-烯烴,是指乙烯、1-丁烯、1-己烯、1-辛烯、1-癸烯、1-十二烯等雙鍵位於α位的烴。另外,本發明中的聚丙烯系樹脂亦可於丙烯單元的莫耳分率不脫離80莫耳%~100莫耳%的範圍的範圍內包含聚對苯二甲酸乙二酯、聚乙烯或聚苯乙烯等其他聚合物。The polypropylene resin in the present invention may contain, for example, a propylene homopolymer, a copolymer of propylene and various α-olefins, etc. Here, the so-called α-olefin refers to a hydrocarbon with a double bond at the α position, such as ethylene, 1-butene, 1-hexene, 1-octene, 1-decene, 1-dodecene, etc. In addition, the polypropylene resin in the present invention may also contain other polymers such as polyethylene terephthalate, polyethylene or polystyrene within a range where the molar fraction of the propylene unit does not deviate from the range of 80 mol% to 100 mol%.

再者,於本發明中,丙烯單元於重複單元中所佔的莫耳分率(莫耳%)是指以如下方式求出者。In the present invention, the molar fraction (mol %) of the propylene unit in the repeating unit is determined as follows.

首先,於自長纖維不織布的任意位置採取的約50 mg的試驗片中加入1 mL的鄰二氯苯/苯-d6的混合溶媒(鄰二氯苯與苯-d6的容積比=9:1),加溫至135℃進行溶解。繼而,對所獲得的溶液進行 13C-核磁共振(nuclear magnetic resonance,NMR)測定,根據NMR光譜來算出起因於丙烯單元的波峰的面積與起因於丙烯單元以外的重複單元的波峰的面積。根據丙烯單元與丙烯單元以外的重複單元的波峰面積比來算出構成聚丙烯系樹脂的所有重複單元中的丙烯單元的莫耳分率(莫耳%),將小數第一位四捨五入。 First, 1 mL of a mixed solvent of o-dichlorobenzene/benzene-d6 (volume ratio of o-dichlorobenzene to benzene-d6 = 9:1) was added to a test piece of about 50 mg taken from an arbitrary position of a long-fiber nonwoven fabric, and the mixture was dissolved by heating to 135°C. Then, the obtained solution was subjected to 13 C-nuclear magnetic resonance (NMR) measurement, and the area of the peak due to the propylene unit and the area of the peak due to the repeating unit other than the propylene unit were calculated from the NMR spectrum. The molar fraction (molar %) of the propylene unit in all the repeating units constituting the polypropylene resin was calculated from the peak area ratio of the propylene unit to the repeating unit other than the propylene unit, and the first decimal place was rounded off.

本發明中的聚丙烯系樹脂亦可包含氧化鈦、二氧化矽、氧化鋇、碳酸鈣等無機物、碳黑、染料或顏料等著色劑、阻燃劑、螢光增白劑、抗氧化劑、帶電穩定劑、抗靜電劑或紫外線吸收劑等各種添加劑。The polypropylene resin of the present invention may also contain various additives such as inorganic substances such as titanium oxide, silicon dioxide, barium oxide, calcium carbonate, carbon black, coloring agents such as dyes or pigments, flame retardants, fluorescent brighteners, antioxidants, charge stabilizers, antistatic agents or ultraviolet absorbers.

於本發明的長纖維不織布中,聚丙烯系樹脂的熔點較佳為140℃以上且170℃以下。熔點為所述範圍內的聚烯烴系樹脂的製成纖維時的強度優異,於製造步驟中不易產生斷紗,因此所獲得的長纖維不織布可獲得缺點少者。In the long fiber nonwoven fabric of the present invention, the melting point of the polypropylene resin is preferably 140° C. or higher and 170° C. or lower. The polyolefin resin having a melting point within the above range has excellent strength when made into fibers, and yarn breakage is less likely to occur during the manufacturing process, so the obtained long fiber nonwoven fabric can be obtained with fewer defects.

再者,本發明中的聚丙烯系樹脂的熔點是指以如下方式求出者。In addition, the melting point of the polypropylene resin in the present invention is determined as follows.

首先,自長纖維不織布的任意位置採取約2 mg並設置於示差掃描熱量計,於氮氣環境下,以升溫速度10℃/分鐘使溫度上升至250℃而進行熔解後,藉由空冷而降溫至20℃。其次,針對再次成為固體的樣品,於氮氣環境下,以升溫速度10℃/分鐘、測定溫度範圍50℃~250℃進行示差掃描熱量測定,將所獲得的測定結果(示差掃描熱量測定(Differential Scanning Calorimetry,DSC)曲線)中的吸熱波峰的頂點的溫度作為熔點。再者,於看到多個吸熱波峰的情況下,將吸熱量最大的波峰的頂點的溫度作為熔點。First, about 2 mg of the long-fiber nonwoven fabric was taken from any position and placed in a differential scanning calorimeter. After melting, the temperature was raised to 250°C at a heating rate of 10°C/min in a nitrogen environment, and then cooled to 20°C by air cooling. Next, the sample that had become solid again was subjected to differential scanning calorimetry in a nitrogen environment at a heating rate of 10°C/min and a measurement temperature range of 50°C to 250°C. The temperature of the top of the endothermic peak in the obtained measurement result (Differential Scanning Calorimetry (DSC) curve) was taken as the melting point. Furthermore, when multiple endothermic peaks were observed, the temperature of the top of the peak with the largest endothermic amount was taken as the melting point.

而且,於本發明的長纖維不織布中,聚丙烯系樹脂的結晶熔解熱量較佳為75 J/g以上且150 J/g以下。結晶熔解熱量為所述範圍內的聚丙烯系樹脂的製成長纖維不織布時的加工性優異,因此較佳。In the long fiber nonwoven fabric of the present invention, the crystallization fusion heat of the polypropylene resin is preferably 75 J/g or more and 150 J/g or less. The polypropylene resin having a crystallization fusion heat within the above range is preferred because it has excellent processability when made into a long fiber nonwoven fabric.

再者,本發明中的聚丙烯系樹脂的結晶熔解熱量分別是指以如下方式求出者。In addition, the crystal fusion heat of the polypropylene resin in the present invention refers to that obtained as follows.

首先,自長纖維不織布的任意位置採取約2 mg並設置於示差掃描熱量計,於氮氣環境下,以升溫速度10℃/分鐘使溫度上升至250℃而進行熔解後,藉由空冷而降溫至20℃。其次,針對再次成為固體的樣品,於氮氣環境下,以升溫速度10℃/分鐘、測定溫度範圍50℃~250℃進行示差掃描熱量測定,根據所獲得的測定結果(DSC曲線)中的吸熱波峰的面積來算出結晶熔解熱量。再者,於看到多個吸熱波峰的情況下,根據將所有的吸熱波峰的面積合算而得的值來算出結晶熔解熱量。First, about 2 mg was collected from an arbitrary position of the long-fiber nonwoven fabric and placed in a differential scanning calorimeter. The sample was melted by heating it up to 250°C at a rate of 10°C/min in a nitrogen atmosphere, and then cooled to 20°C by air cooling. Next, the sample that had become solid again was subjected to differential scanning calorimetry in a nitrogen atmosphere at a rate of 10°C/min in a measurement temperature range of 50°C to 250°C. The crystal melting heat was calculated from the area of the endothermic peak in the obtained measurement result (DSC curve). Furthermore, when multiple endothermic peaks were observed, the crystal melting heat was calculated from the value obtained by adding up the areas of all the endothermic peaks.

本發明中的聚丙烯系樹脂較佳為Mw為20000以上且120000以下。藉由使Mw較佳為20000以上、更佳為25000以上、進而佳為30000以上,於紡紗步驟中不易產生斷紗。另一方面,藉由使Mw較佳為120000以下、更佳為100000以下、進而佳為80000以下,從而形成容易加工成積層體的柔軟的不織布。The polypropylene resin in the present invention preferably has an Mw of 20,000 or more and 120,000 or less. By setting the Mw to preferably 20,000 or more, more preferably 25,000 or more, and further preferably 30,000 or more, yarn breakage is less likely to occur in the spinning step. On the other hand, by setting the Mw to preferably 120,000 or less, more preferably 100,000 or less, and further preferably 80,000 or less, a soft nonwoven fabric that is easily processed into a laminate can be formed.

本發明中的聚丙烯系樹脂較佳為Mw/Mn為2.00以上且4.00以下。藉由使Mw/Mn較佳為2.00以上、更佳為2.20以上、進而佳為2.40以上、尤佳為2.60以上,實施壓花加工時的接著性提高。另一方面,藉由使Mw/Mn較佳為4.00以下、更佳為3.90以下、進而佳為3.80以下,製成長纖維不織布時的品位提高。The polypropylene resin in the present invention preferably has an Mw/Mn of 2.00 or more and 4.00 or less. By making Mw/Mn preferably 2.00 or more, more preferably 2.20 or more, further preferably 2.40 or more, and particularly preferably 2.60 or more, the adhesion during embossing is improved. On the other hand, by making Mw/Mn preferably 4.00 or less, more preferably 3.90 or less, and further preferably 3.80 or less, the quality of long fiber nonwoven fabric is improved.

再者,於本發明中,Mw、Mn是指藉由以下方法來測定而算出的值。 (1) 自長纖維不織布的端部除外的區域隨機採取5點試驗片各5 mg。再者,所謂長纖維不織布的端部,是指相對於長纖維不織布的寬度方向上的長度而為兩端的10%的區域。 (2) 藉由在(1)中所獲得的試驗片中加入1,2,4-三氯苯(例如,富士軟片和光純藥股份有限公司製造者等)5 mL,於165℃下加熱20分鐘來進行溶解。繼而,使所述溶液通過聚四氟乙烯(Polytetrafluoroethylene,PTFE)過濾器(孔徑:0.45 μm)來進行過濾,從而製作試樣溶液。此處,PTFE過濾器例如可使用愛多邦得科(Advantec)東洋股份有限公司製造的「T010A」等。 (3) 針對(2)中所獲得的試樣溶液,於以下條件下使用凝膠滲透層析法(以下,有時記為GPC)進行測定,例如使用懷亞特技術(Wyatt Technology)製造的「埃姆帕瓦(Empower)」等進行GPC中的溶出曲線的解析,藉此求出Mw、Mn。 ‧裝置:例如聚合物實驗室(Polymer Laboratories)公司製造的「PL-220」等 ‧檢測器:示差折射率檢測器RI ‧管柱:Shodex HT-G(保護管柱(guard column))+Shodex HT-806M×2根(8.0 mm×30 cm、例如昭和電工股份有限公司製造者等) ‧溶媒:1,2,4-三氯苯(添加0.1%BHT) ‧流速:1.0 mL/分鐘 ‧管柱溫度:145℃ ‧注入量:0.20 mL ‧標準試樣:單分散聚苯乙烯(例如,東曹股份有限公司製造者等)、聯苄(例如,東京化成工業股份有限公司製造者等)。 In the present invention, Mw and Mn refer to values calculated by the following method. (1) Randomly sample 5 test pieces of 5 mg each from the region excluding the ends of the long fiber nonwoven fabric. The ends of the long fiber nonwoven fabric refer to the region that is 10% of the length of the long fiber nonwoven fabric in the width direction. (2) Add 5 mL of 1,2,4-trichlorobenzene (for example, manufactured by Fuji Films and Kou Pure Chemical Industries, Ltd.) to the test piece obtained in (1), and heat at 165°C for 20 minutes to dissolve. Next, the solution is filtered through a polytetrafluoroethylene (PTFE) filter (pore size: 0.45 μm) to prepare a sample solution. Here, the PTFE filter can be, for example, "T010A" manufactured by Advantec Toyo Co., Ltd. (3) The sample solution obtained in (2) is measured using gel permeation chromatography (hereinafter sometimes referred to as GPC) under the following conditions, for example, using "Empower" manufactured by Wyatt Technology to analyze the elution curve in GPC, thereby determining Mw and Mn. ‧ Apparatus: e.g. "PL-220" manufactured by Polymer Laboratories, Inc. ‧ Detector: Differential refractive index detector RI ‧ Column: Shodex HT-G (guard column) + Shodex HT-806M × 2 pieces (8.0 mm × 30 cm, e.g. manufactured by Showa Denko Co., Ltd., etc.) ‧ Solvent: 1,2,4-trichlorobenzene (with 0.1% BHT added) ‧ Flow rate: 1.0 mL/min ‧ Column temperature: 145°C ‧ Injection volume: 0.20 mL ‧ Standard sample: Monodisperse polystyrene (e.g. manufactured by Tosoh Co., Ltd., etc.), bibenzyl (e.g. manufactured by Tokyo Chemical Industry Co., Ltd., etc.)

[纖維] 本發明的長纖維不織布包括包含所述聚丙烯系樹脂的纖維。而且,該纖維的平均纖維徑為0.05 μm以上且5.00 μm以下。藉由該平均纖維徑的範圍的下限為0.05 μm以上,較佳為0.08 μm以上,更佳為0.20 μm以上,從而形成拉伸強度更高且捲取或捲出等時的步驟穩定性優異的長纖維不織布。另一方面,藉由平均纖維徑的範圍的上限為5.00 μm以下,較佳為2.00 μm以下,更佳為1.00 μm以下,進而佳為0.50 μm以下,長纖維不織布的比表面積增大,從而形成粒子的捕集效率優異的長纖維不織布。 [Fiber] The long-fiber nonwoven fabric of the present invention includes fibers containing the polypropylene resin. Moreover, the average fiber diameter of the fibers is greater than 0.05 μm and less than 5.00 μm. By setting the lower limit of the range of the average fiber diameter to greater than 0.05 μm, preferably greater than 0.08 μm, and more preferably greater than 0.20 μm, a long-fiber nonwoven fabric having higher tensile strength and excellent stability during winding or unwinding is formed. On the other hand, by setting the upper limit of the average fiber diameter range to 5.00 μm or less, preferably 2.00 μm or less, more preferably 1.00 μm or less, and further preferably 0.50 μm or less, the specific surface area of the long fiber nonwoven fabric is increased, thereby forming a long fiber nonwoven fabric with excellent particle collection efficiency.

再者,本發明中的纖維的平均纖維徑(μm)是指如下值,即自從長纖維不織布的寬度方向上的3點(側端部2點與中央1點)各點起於長度方向上以5 cm為間隔各取5點而得的合計15點切出10 mm×5 mm的測定樣品,使用掃描式電子顯微鏡(scanning electron microscope)(SEM、例如日立高新技術(Hitachi High-technologies)股份有限公司製造的「S-5500」等),自所切出的測定樣品以倍率5000倍分別拍攝長纖維不織布的表面照片各1張而獲得合計15張。針對照片中的纖維中可清楚確認到纖維側面的寬度的所有纖維,測定其寬度(μm),將算術平均所得的值的小數第三位四捨五入而獲得的值。再者,即便纖維的剖面形狀為扁平剖面或異形剖面,亦如上所述般將纖維側面的寬度視為纖維徑來進行測定。Furthermore, the average fiber diameter (μm) of the fiber in the present invention refers to the following value, that is, from 3 points in the width direction of the long fiber non-woven fabric (2 points at the side ends and 1 point in the center) each point in the length direction at intervals of 5 cm, a total of 15 points are cut out to obtain a measurement sample of 10 mm×5 mm, and a scanning electron microscope (SEM, such as "S-5500" manufactured by Hitachi High-technologies Co., Ltd.) is used. Photographs of the surface of the long fiber non-woven fabric are taken one by one from the cut measurement sample at a magnification of 5000 times, and a total of 15 photos are obtained. For all fibers in the photograph whose fiber side widths can be clearly confirmed, the widths (μm) are measured, and the arithmetic average of the values is rounded off to the third decimal place. Even if the cross-sectional shape of the fiber is a flat cross-section or an irregular cross-section, the width of the fiber side is regarded as the fiber diameter for measurement as described above.

構成本發明的長纖維不織布的纖維可為扁平剖面或異形剖面,較佳為圓剖面。藉由設為圓剖面,紡紗性提高,不易產生斷紗。The fibers constituting the long-fiber nonwoven fabric of the present invention may have a flat cross section or an irregular cross section, preferably a round cross section. By setting the cross section to a round cross section, the spinnability is improved and yarn breakage is less likely to occur.

[長纖維不織布] 本發明的長纖維不織布包含所述纖維。而且,所謂本發明中所述的「長纖維不織布」,是指藉由後述的製造方法而製造的熔噴不織布或紡黏不織布等不織布,且是將僅包含切割成一定長度(例如,100 mm)的纖維的不織布(短纖維不織布)除外者。 [Long-fiber nonwoven fabric] The long-fiber nonwoven fabric of the present invention includes the above-mentioned fibers. Moreover, the "long-fiber nonwoven fabric" described in the present invention refers to a nonwoven fabric such as a meltblown nonwoven fabric or a spunbonded nonwoven fabric produced by the production method described below, and excludes a nonwoven fabric (short-fiber nonwoven fabric) containing only fibers cut into a certain length (e.g., 100 mm).

本發明的長纖維不織布於190℃的零剪切黏度為5 Pa·s以上且10 Pa·s以下。藉由該零剪切黏度的範圍的下限為5 Pa·s以上,較佳為6.0 Pa·s以上,從而形成具有高拉伸強度的纖維,即便製成長纖維不織布,拉伸強度亦高。另一方面,藉由零剪切黏度的範圍的上限為10 Pa·s以下,較佳為9.0 Pa·s以下,從而形成具有高通氣性的長纖維不織布。The zero shear viscosity of the long fiber nonwoven fabric of the present invention at 190°C is 5 Pa·s or more and 10 Pa·s or less. By setting the lower limit of the zero shear viscosity range to 5 Pa·s or more, preferably 6.0 Pa·s or more, a fiber having high tensile strength is formed, and even if a long fiber nonwoven fabric is made, the tensile strength is high. On the other hand, by setting the upper limit of the zero shear viscosity range to 10 Pa·s or less, preferably 9.0 Pa·s or less, a long fiber nonwoven fabric having high air permeability is formed.

再者,於本發明中,所謂長纖維不織布的零剪切黏度,是指以如下方式測定而算出的值。 (1) 自長纖維不織布的任意位置採取2張試驗片。此時,所採取的量設為足以填充於後述的流變儀的平行板間的量,即足以填充底面的半徑為10 mm、高度為0.5 mm的圓柱的量。該量至少為0.15 g,結合測定裝置的規格來調整。 (2) 使用設定為190℃的流變儀(例如,UBM股份有限公司製造的「萊奧索爾(Reosol)G3000」等),設置設有所述試驗片1張的平行板,分別測定以角頻率1.26 rad/sec、3.14 rad/sec、6.28 rad/sec、12.57 rad/sec、31.42 rad/sec、62.83 rad/sec賦予應變時的熔融黏度。對另1張試驗片亦同樣地測定。 (3) 對自2張試驗片獲得的結果按各角頻率平均而得的值與角頻率的關係進行線性近似。 (4) 將藉由使由線性近似獲得的近似式外推至0 rad/sec而算出的熔融黏度的值作為零剪切黏度。 Furthermore, in the present invention, the zero shear viscosity of the long-fiber nonwoven fabric refers to the value calculated by measuring as follows. (1) Take two test pieces from any position of the long-fiber nonwoven fabric. At this time, the amount taken is set to be sufficient to fill the space between the parallel plates of the rheometer described later, that is, the amount sufficient to fill a cylinder with a bottom radius of 10 mm and a height of 0.5 mm. The amount is at least 0.15 g and is adjusted in combination with the specifications of the measuring device. (2) Using a rheometer set at 190°C (e.g., "Reosol G3000" manufactured by UBM Co., Ltd.), a parallel plate with one of the test pieces is set, and the melt viscosity is measured when strain is applied at angular frequencies of 1.26 rad/sec, 3.14 rad/sec, 6.28 rad/sec, 12.57 rad/sec, 31.42 rad/sec, and 62.83 rad/sec. The other test piece is measured in the same manner. (3) The relationship between the value obtained by averaging the results obtained from the two test pieces at each angular frequency and the angular frequency is linearly approximated. (4) The value of the melt viscosity calculated by extrapolating the approximate formula obtained by the linear approximation to 0 rad/sec is taken as the zero shear viscosity.

另外,本發明的長纖維不織布於190℃的零剪切黏度可藉由聚丙烯系樹脂的熔體流動速率或分子量分佈、或後述的有機過氧化物的添加形態(是否使用母料等)、用以使聚丙烯系樹脂與有機過氧化物反應的擠出機的溫度、或有機過氧化物的種類等來控制。In addition, the zero shear viscosity of the long fiber nonwoven fabric of the present invention at 190°C can be controlled by the melt flow rate or molecular weight distribution of the polypropylene resin, the addition form of the organic peroxide described later (whether a masterbatch is used, etc.), the temperature of the extruder for reacting the polypropylene resin with the organic peroxide, or the type of the organic peroxide.

本發明的長纖維不織布較佳為以100 ppm以上且1000 ppm以下的比例含有具有以下的通式(1)或通式(2)所表示的結構的有機過氧化物。The long-fiber nonwoven fabric of the present invention preferably contains an organic peroxide having a structure represented by the following general formula (1) or (2) in a ratio of 100 ppm to 1000 ppm.

[化5] [Chemistry 5]

[化6] [Chemistry 6]

此處,R 1~R 3、R 5~R 7為碳原子數1~10的烷基、烯基、苯基、苄基或苯甲醯基,R 4、R 8為碳原子數1~20且除碳原子以外僅包含氫原子的結構。 Here, R 1 to R 3 and R 5 to R 7 are alkyl, alkenyl, phenyl, benzyl or benzoyl groups having 1 to 10 carbon atoms, and R 4 and R 8 are structures having 1 to 20 carbon atoms and containing only hydrogen atoms other than carbon atoms.

藉由所述有機過氧化物的含量的範圍的下限較佳為100 ppm以上,更佳為120 ppm以上,進而佳為150 ppm以上,從而形成體積更大且通氣性優異的長纖維不織布。另一方面,藉由所述含量的範圍的上限較佳為1000 ppm以下,更佳為750 ppm以下,進而佳為500 ppm以下,從而形成粒子的捕集性能優異的長纖維不織布。The lower limit of the content of the organic peroxide is preferably 100 ppm or more, more preferably 120 ppm or more, and further preferably 150 ppm or more, thereby forming a long-fiber nonwoven fabric with a larger volume and excellent air permeability. On the other hand, the upper limit of the content is preferably 1000 ppm or less, more preferably 750 ppm or less, and further preferably 500 ppm or less, thereby forming a long-fiber nonwoven fabric with excellent particle capture performance.

作為所述有機過氧化物,可列舉:「二-第三丁基過氧化物、二異丙苯過氧化物、2,5-二甲基-2,5-雙(第三丁基過氧化)己烷、2,5-二甲基-2,5-雙(第三丁基過氧化)己炔-3、α,α'-雙(第三丁基過氧化)二異丙基苯」等二烷基過氧化物類、或「1,1-雙(第三丁基過氧化)-3,3,5-三甲基環己烷、2,2-雙(第三丁基過氧化)丁烷」等過氧化縮酮類等。Examples of the organic peroxide include dialkyl peroxides such as "di-tert-butyl peroxide, diisopropylbenzene peroxide, 2,5-dimethyl-2,5-bis(tert-butylperoxide)hexane, 2,5-dimethyl-2,5-bis(tert-butylperoxide)hexyne-3, α,α'-bis(tert-butylperoxide)diisopropylbenzene", and peroxyketal such as "1,1-bis(tert-butylperoxide)-3,3,5-trimethylcyclohexane, 2,2-bis(tert-butylperoxide)butane".

再者,於本發明中,所述有機過氧化物的含量是指藉由以下方法來測定而算出的值。 (1) 自長纖維不織布的端部除外的區域隨機採取5點試驗片各25 mg。再者,所謂不織布的端部,是指相對於不織布的寬度方向上的長度而為兩端的10%的區域。 (2) 將(1)中所獲得的試驗片浸漬於體積比率設為1:1的氯仿/甲醇溶媒中,於15分鐘、45 kHz的條件下進行超音波處理並加以溶解。於該超音波處理中例如可使用亞速旺(ASONE)股份有限公司製造的超音波清洗器「VS-100 III」等。另外,所述溶媒相對於試驗片的質量的量設為以相對於試驗片1 mg而溶媒為0.8 mL進行。 (3) 利用聚四氟乙烯(PTFE)製的過濾器(以後,有時簡記為「PTFE過濾器」;孔徑:0.45 μm)對(2)中所獲得的超音波處理後的溶液進行過濾,製成試樣溶液。此處,PTFE過濾器例如可使用愛多邦得科(Advantec)東洋股份有限公司製造的「T010A」等。 (4) 將有機過氧化物0.1 g溶解於體積比率設為1:1的氯仿/甲醇溶液10 mL中,製備標準原液(10 μg/mL)。然後,藉由利用所述氯仿/甲醇溶液稀釋該標準原液而製備各濃度(0.1 μg/mL、0.2 μg/mL、0.5 μg/mL、1.0 μg/mL)的標準溶液。此時,作為所述有機過氧化物,可列舉下述者,針對各者,製備各濃度的標準溶液。另外,於藉由其他方法(例如,碘滴定法、極譜法等)而明確含有下述有機過氧化物以外的具有所述通式(1)或通式(2)所表示的結構的有機過氧化物的情況或者推測至少含有的情況下,亦製備該有機過氧化物的標準溶液。 ‧二-第三丁基過氧化物 ‧二異丙苯過氧化物 ‧2,5-二甲基-2,5-雙(第三丁基過氧化)己烷 ‧2,5-二甲基-2,5-雙(第三丁基過氧化)己炔-3 ‧α,α'-雙(第三丁基過氧化)二異丙基苯 ‧1,1-雙(第三丁基過氧化)-3,3,5-三甲基環己烷 ‧2,2-雙(第三丁基過氧化)丁烷 (5) 使用所述試樣溶液,於以下條件下供於液相層析質譜(Liquid Chromatography-Tandem Mass Spectrometry,LC/MS/MS)。 ‧高效液相層析儀(high performance liquid chromatograph,HPLC):例如島津製作所股份有限公司製造的「LC-20A」等 ‧質譜計(mass spectrometer,MS):例如薩依埃克斯(Sciex)製造的「API4000」等 ‧管柱:ODS系管柱(例如,住化分析中心股份有限公司製造的「薩米帕克斯(SUMIPAX)ODS A系列」等) ‧流動相:0.1%甲酸水溶液+甲醇(梯度萃取條件) ‧注入量:5 μL ‧離子化:電灑游離法(electrospray ionization,ESI) (6) 根據各試樣溶液的質譜(MS)來鑑定有機過氧化物,使用根據所述有機過氧化物的標準溶液而獲得的校準曲線,根據波峰面積來定量有機過氧化物量(ppm)。 (7) 將對各試驗片測定而得的值的算術平均值(ppm)的小數點以下第一位四捨五入,求出有機過氧化物量(ppm)。 Furthermore, in the present invention, the content of the organic peroxide refers to a value calculated by the following method. (1) Randomly take 5 test pieces of 25 mg each from the area excluding the end of the long fiber nonwoven fabric. Furthermore, the end of the nonwoven fabric refers to an area that is 10% of the length of the two ends relative to the length in the width direction of the nonwoven fabric. (2) The test piece obtained in (1) is immersed in a chloroform/methanol solvent with a volume ratio of 1:1, and ultrasonically treated and dissolved under the conditions of 45 kHz for 15 minutes. For the ultrasonic treatment, for example, the ultrasonic cleaner "VS-100 III" manufactured by ASONE Co., Ltd. can be used. In addition, the amount of the solvent relative to the mass of the test piece is set to 0.8 mL of the solvent relative to 1 mg of the test piece. (3) The solution obtained after the ultrasonic treatment in (2) is filtered using a filter made of polytetrafluoroethylene (PTFE) (hereinafter, sometimes referred to as "PTFE filter"; pore size: 0.45 μm) to prepare a sample solution. Here, the PTFE filter can be, for example, "T010A" manufactured by Advantec Toyo Co., Ltd. (4) 0.1 g of an organic peroxide is dissolved in 10 mL of a chloroform/methanol solution with a volume ratio of 1:1 to prepare a standard stock solution (10 μg/mL). Then, the standard stock solution is diluted with the chloroform/methanol solution to prepare standard solutions of various concentrations (0.1 μg/mL, 0.2 μg/mL, 0.5 μg/mL, 1.0 μg/mL). At this time, the following can be listed as the organic peroxides, and standard solutions of various concentrations are prepared for each. In addition, when an organic peroxide having a structure represented by the general formula (1) or (2) other than the organic peroxide described below is clearly contained by other methods (e.g., iodine titration, polarography, etc.) or is estimated to be contained, a standard solution of the organic peroxide is also prepared. ‧Di-tert-butyl peroxide ‧Diisopropylbenzene peroxide ‧2,5-Dimethyl-2,5-bis(tert-butyl peroxide)hexane ‧2,5-Dimethyl-2,5-bis(tert-butyl peroxide)hexyne-3 ‧α,α'-bis(tert-butyl peroxide)diisopropylbenzene ‧1,1-bis(tert-butyl peroxide)-3,3,5-trimethylcyclohexane ‧2,2-bis(tert-butyl peroxide)butane (5) The sample solution was subjected to liquid chromatography-tandem mass spectrometry (LC/MS/MS) under the following conditions. ‧High performance liquid chromatograph (HPLC): such as "LC-20A" manufactured by Shimadzu Corporation ‧Mass spectrometer (MS): such as "API4000" manufactured by Sciex ‧Column: ODS series column (such as "SUMIPAX ODS A series" manufactured by Sumika Analytical Center Co., Ltd.) ‧Mobile phase: 0.1% formic acid aqueous solution + methanol (gradient extraction conditions) ‧Injection volume: 5 μL ‧Ionization: electrospray ionization (ESI) (6) Organic peroxides were identified based on the mass spectrum (MS) of each sample solution, and the amount of organic peroxides (ppm) was quantified based on the peak area using a calibration curve obtained based on a standard solution of the organic peroxide. (7) The arithmetic mean (ppm) of the values measured for each test piece was rounded off to the first decimal point to calculate the amount of organic peroxides (ppm).

構成本發明的長纖維不織布的聚丙烯系樹脂中的有機過氧化物的含量可藉由有機過氧化物的添加形態及添加溫度來控制。The content of organic peroxide in the polypropylene resin constituting the long-fiber nonwoven fabric of the present invention can be controlled by the addition form and addition temperature of the organic peroxide.

本發明的長纖維不織布較佳為單位面積重量為5 g/m 2以上且100 g/m 2以下。藉由長纖維不織布的單位面積重量較佳為5 g/m 2以上,更佳為7 g/m 2以上,進而佳為10 g/m 2以上,從而形成拉伸強度更高的長纖維不織布。另外,藉由長纖維不織布的單位面積重量較佳為100 g/m 2以下,更佳為70 g/m 2以下,進而佳為50 g/m 2以下,從而形成容易進行積層加工或縫製加工等的長纖維不織布。 The long fiber nonwoven fabric of the present invention preferably has a unit area weight of 5 g/ m2 or more and 100 g/ m2 or less. By having a unit area weight of the long fiber nonwoven fabric preferably of 5 g/ m2 or more, more preferably of 7 g/ m2 or more, and further preferably of 10 g/ m2 or more, a long fiber nonwoven fabric with higher tensile strength is formed. In addition, by having a unit area weight of the long fiber nonwoven fabric preferably of 100 g/ m2 or less, more preferably of 70 g/ m2 or less, and further preferably of 50 g/ m2 or less, a long fiber nonwoven fabric that is easy to perform lamination processing or sewing processing is formed.

再者,本發明中的不織布的單位面積重量(g/m 2)是基於日本工業標準(Japanese Industrial Standards,JIS)L1913:2010「通常不織布試驗方法」的「6.2 每單位面積的質量」而求出。 The weight per unit area (g/m 2 ) of the nonwoven fabric in the present invention is determined based on "6.2 Mass per unit area" of "General nonwoven fabric test methods" of Japanese Industrial Standards (JIS) L1913:2010.

自不織布切出20 cm×25 cm的試驗片,不織布的寬度每1 m採取3張並秤量標準狀態下的各自的質量(g),根據所測定的值的算術平均來算出每1 m 2的質量(g/m 2),將小數點第一位四捨五入。 Cut a 20 cm x 25 cm test piece from the nonwoven fabric. Take three pieces per 1 m of the nonwoven fabric width and weigh the mass (g) of each piece in the standard state. Calculate the mass per 1 m2 (g/ m2 ) from the arithmetic mean of the measured values, rounding off to the first decimal place.

本發明的長纖維不織布較佳為空隙率為92.5%以上且99.0%以下。藉由將空隙率設為92.5%以上,長纖維不織布的通氣性提高。另一方面,若空隙率超過99.0%,則強度下降而欠佳。The long fiber nonwoven fabric of the present invention preferably has a porosity of 92.5% or more and 99.0% or less. By setting the porosity to 92.5% or more, the air permeability of the long fiber nonwoven fabric is improved. On the other hand, if the porosity exceeds 99.0%, the strength decreases and is not preferred.

此處,本發明中的不織布的空隙率(%)是指以如下方式求出者。Here, the void ratio (%) of the nonwoven fabric in the present invention is determined as follows.

首先,以如下方式求出不織布的厚度(μm)。使用3D顯微鏡(例如,基恩士(KEYENCE)股份有限公司製造的「VR-3050」等),以倍率12倍以於圖像整體中拍有不織布的方式拍攝不織布表面的高度像,求出圖像的各畫素(x,y)距試樣台的高度T(x,y)(μm)。將所有的畫素的T(x,y)平均而得者作為不織布的厚度。其次,將如下值,即使用利用所述方法求出的單位面積重量與厚度、不織布中所使用的原料的密度並根據以下式而求出的值的小數第二位四捨五入。 空隙率(%)=〔1-(單位面積重量/厚度/密度)〕×100 First, the thickness (μm) of the nonwoven fabric is calculated as follows. Use a 3D microscope (e.g., "VR-3050" manufactured by KEYENCE Co., Ltd.) to take a height image of the nonwoven fabric surface at a magnification of 12 times so that the nonwoven fabric is captured in the entire image, and calculate the height T (x, y) (μm) of each pixel (x, y) of the image from the sample stand. The average of T (x, y) of all pixels is taken as the thickness of the nonwoven fabric. Next, the following value, which is the value calculated according to the following formula using the unit area weight and thickness calculated using the above method and the density of the raw material used in the nonwoven fabric, is rounded to the second decimal place. Porosity (%) = [1-(unit area weight/thickness/density)] × 100

本發明的長纖維不織布可實施駐極體加工。藉由後述的方法來實施駐極體加工,藉此可不損及通氣性地提高粒子的捕集效率。The long fiber nonwoven fabric of the present invention can be subjected to a stationary electrode treatment. By conducting the stationary electrode treatment by the method described below, the particle collection efficiency can be improved without compromising the air permeability.

[長纖維不織布的製造方法] 其次,對製造本發明的長纖維不織布的較佳態樣進行具體說明,但本發明並不限定於此。 [Manufacturing method of long-fiber nonwoven fabric] Next, the preferred method for manufacturing the long-fiber nonwoven fabric of the present invention will be specifically described, but the present invention is not limited thereto.

本發明的長纖維不織布的製造方法較佳為具有:將於溶體流動速率為500 g/10分鐘以上且2000 g/10分鐘以下的聚丙烯系樹脂(以下,稱為原料樹脂)中添加具有所述通式(1)或通式(2)所表示的結構的有機過氧化物而得的原料樹脂組成物熔融而獲得熔融樹脂的步驟;以及對所述熔融樹脂施加熔噴法而獲得長纖維不織布的步驟。The method for producing the long-fiber nonwoven fabric of the present invention preferably comprises: a step of melting a raw material resin composition obtained by adding an organic peroxide having a structure represented by the general formula (1) or (2) to a polypropylene resin having a melt flow rate of 500 g/10 minutes or more and 2000 g/10 minutes or less (hereinafter referred to as the raw material resin) to obtain a molten resin; and a step of subjecting the molten resin to a melt spraying method to obtain a long-fiber nonwoven fabric.

(a)將於原料樹脂中添加有機過氧化物而得的原料樹脂組成物熔融而獲得熔融樹脂的步驟 於本發明的長纖維不織布的製造方法中,首先,於原料樹脂中添加有機過氧化物,將該原料樹脂分解而獲得熔融樹脂。此時所使用的原料樹脂較佳為熔體流動速率(以下,有時記為MFR)為500 g/10分鐘以上且2000 g/10分鐘以下。MFR未滿500 g/10分鐘的聚丙烯系樹脂由於分解該聚丙烯系樹脂所需的有機過氧化物的添加量變多,因此未反應而殘存的有機過氧化物變得過多,因此於紡紗時頻發斷紗,製成長纖維不織布時的品位降低。另外,MFR超過2000 g/10分鐘的聚丙烯系樹脂通常以粉體或蠟狀的形態提供,因此於擠出機中難以操作,與碎片或顆粒形態者相比,供給變得不穩定,紡紗性有時降低。 (a) A step of melting a raw resin composition obtained by adding an organic peroxide to a raw resin to obtain a molten resin In the method for producing a long-fiber nonwoven fabric of the present invention, first, an organic peroxide is added to a raw resin to decompose the raw resin to obtain a molten resin. The raw resin used at this time preferably has a melt flow rate (hereinafter, sometimes referred to as MFR) of 500 g/10 minutes or more and 2000 g/10 minutes or less. For a polypropylene resin having an MFR of less than 500 g/10 minutes, the amount of organic peroxide added to decompose the polypropylene resin increases, and thus the amount of organic peroxide remaining without reaction becomes excessive, so that yarn breakage occurs frequently during spinning, and the quality of the long-fiber nonwoven fabric is reduced. In addition, polypropylene resins with an MFR exceeding 2000 g/10 minutes are usually provided in the form of powder or wax, which makes them difficult to handle in an extruder. Compared with those in the form of chips or pellets, the supply becomes unstable and the spinnability may be reduced.

再者,於本發明中,聚丙烯系樹脂的熔體流動速率(g/10分鐘)是指如下值,即基於JIS K7210-1:2014「塑膠-熱塑性塑膠的熔體質量流動速率(melt mass-flow rate)(MFR)及熔體體積流動速率(melt volume-flow rate,MVR)的求法-第一部:標準的試驗方法」的「8 A法:質量測定法」,於溫度230℃、荷重2.16 kg、測定時間10分鐘的條件下測定而得的值。In the present invention, the melt flow rate (g/10 minutes) of the polypropylene resin refers to the following value, which is measured under the conditions of a temperature of 230°C, a load of 2.16 kg, and a measurement time of 10 minutes based on "8 A method: Mass measurement method" of JIS K7210-1:2014 "Plastics-Method for determining melt mass flow rate (MFR) and melt volume flow rate (MVR) of thermoplastic plastics-Part 1: Standard test methods".

另外,於本發明的長纖維不織布的製造方法中所使用的原料樹脂中,可於不損及本發明的效果的範圍內添加氧化鈦、二氧化矽、氧化鋇、碳酸鈣等無機物、碳黑、染料或顏料等著色劑、阻燃劑、螢光增白劑、抗氧化劑、帶電穩定劑、抗靜電劑或紫外線吸收劑等各種添加劑。In addition, various additives such as titanium oxide, silicon dioxide, barium oxide, calcium carbonate and other inorganic substances, carbon black, dyes or pigments and other coloring agents, flame retardants, fluorescent whitening agents, antioxidants, charge stabilizers, antistatic agents or ultraviolet absorbers may be added to the raw material resin used in the method for producing the long-fiber nonwoven fabric of the present invention within the range that does not impair the effects of the present invention.

作為本發明的長纖維不織布的製造方法中所使用的有機過氧化物,可列舉[長纖維不織布]中記載的有機過氧化物。Examples of the organic peroxide used in the method for producing the long-fiber nonwoven fabric of the present invention include organic peroxides described in [Long-fiber nonwoven fabric].

於原料樹脂中添加所述有機過氧化物並使該原料樹脂分解而獲得的熔融樹脂可不特別進行乾燥等地供於後述的「實施熔噴法而獲得長纖維不織布的步驟」。The molten resin obtained by adding the organic peroxide to the raw material resin and decomposing the raw material resin can be provided to the "step of obtaining a long-fiber nonwoven fabric by melt-blowing" described later without being particularly dried.

而且,作為於原料樹脂中添加所述有機過氧化物而獲得熔融樹脂的方法,較佳為於用以向紡紗機中供給原料的擠出機內反應的方法。此處,所謂紡紗機,是指後述的「實施熔噴法而獲得長纖維不織布的步驟」中使用的紡紗機。例如,藉由乾式摻合或分別測量而將原料樹脂與所述有機過氧化物同時投入至擠出機中,利用用以向紡紗機中供給原料的擠出機進行混練,藉此可連續地獲得於原料樹脂中添加有機過氧化物而得的熔融樹脂,並連續地向紡紗機中供給原料,從而可簡化步驟。作為添加原料樹脂與所述有機過氧化物而獲得熔融樹脂的其他方法,有如下方法等:於投入至用以向紡紗機中供給原料的擠出機中前,事先利用獨立於紡紗機的擠出機於原料樹脂中混練有機過氧化物並加以顆粒化,將該顆粒投入至用以向紡紗機中供給原料的擠出機中進行熔融。Furthermore, as a method for obtaining a molten resin by adding the organic peroxide to a raw material resin, a method of reacting in an extruder for supplying raw materials to a spinning machine is preferred. Here, the so-called spinning machine refers to the spinning machine used in the "step of obtaining a long-fiber nonwoven fabric by melt-blowing method" described later. For example, the raw material resin and the organic peroxide are simultaneously introduced into an extruder by dry blending or separate measurement, and kneaded by an extruder for supplying raw materials to a spinning machine, thereby continuously obtaining a molten resin obtained by adding an organic peroxide to a raw material resin, and continuously supplying the raw materials to the spinning machine, thereby simplifying the steps. As another method for obtaining a molten resin by adding a raw material resin and the organic peroxide, there is a method in which an organic peroxide is kneaded and granulated in a raw material resin by an extruder independent of a spinning machine before being fed into an extruder for feeding a raw material into a spinning machine, and the granules are fed into an extruder for feeding a raw material into a spinning machine to be melted.

於將原料樹脂與所述有機過氧化物同時投入至擠出機中進行混練的情況下,擠出機的溫度較佳為(原料樹脂的熔點+20℃)以上且(原料樹脂的熔點+60℃)以下。即,可以說大致180℃~220℃是較佳的範圍。藉由將擠出機的溫度設為所述範圍內,於擠出機內對原料施加大的剪切力,原料樹脂與有機過氧化物容易均勻地混練,因此可使有機過氧化物更有效率地發揮作用。When the raw material resin and the organic peroxide are simultaneously introduced into an extruder for kneading, the temperature of the extruder is preferably not less than (melting point of the raw material resin + 20°C) and not more than (melting point of the raw material resin + 60°C). That is, it can be said that approximately 180°C to 220°C is a preferable range. By setting the temperature of the extruder within the above range, a large shear force is applied to the raw material in the extruder, and the raw material resin and the organic peroxide are easily and uniformly kneaded, so that the organic peroxide can function more efficiently.

另外,所述有機過氧化物較佳為事先與聚丙烯系樹脂混練來製造母料,將該母料添加於原料樹脂中而獲得熔融樹脂。作為用以製造母料的聚丙烯系樹脂,可使用與原料樹脂相同的聚丙烯系樹脂。藉由製成母料的形態後添加,有機過氧化物不易偏在化,即便進行短時間混練,亦可使聚丙烯系樹脂均勻地低黏度化。In addition, the organic peroxide is preferably kneaded with a polypropylene resin in advance to prepare a masterbatch, and the masterbatch is added to the raw resin to obtain a molten resin. As the polypropylene resin used to prepare the masterbatch, the same polypropylene resin as the raw resin can be used. By adding the organic peroxide in the form of a masterbatch, it is difficult for the organic peroxide to be localized, and even if the kneading is performed for a short time, the viscosity of the polypropylene resin can be uniformly reduced.

所述原料樹脂中的有機過氧化物的添加量較佳為原料整體的0.20質量%以上且1.0質量%以下。藉由使添加量較佳為0.20質量%以上,即便於藉由乾式摻合進行添加的情況下,亦可使聚丙烯系樹脂效率良好地低黏度化。另一方面,藉由使添加量較佳為1.0質量%以下、更佳為0.90質量%以下、進而佳為0.80質量%以下,紡紗性提高,從而可獲得品位高的長纖維不織布。The amount of organic peroxide added to the raw material resin is preferably 0.20 mass% or more and 1.0 mass% or less of the total raw material. By setting the added amount to 0.20 mass% or more, even when adding by dry blending, the viscosity of the polypropylene resin can be efficiently reduced. On the other hand, by setting the added amount to 1.0 mass% or less, more preferably 0.90 mass% or less, and further preferably 0.80 mass% or less, the spinnability is improved, thereby obtaining a high-quality long-fiber nonwoven fabric.

本發明中的紡紗溫度較佳為設為(原料樹脂的熔解溫度+30℃)以上且(原料樹脂的熔點+160℃)以下。即,可以說大致190℃~320℃是較佳的範圍。藉由使紡紗溫度較佳為190℃以上,所紡出的熔融樹脂的黏度降低,可促進纖維的極細化。另外,藉由使紡紗溫度較佳為320℃以下、更佳為300℃以下,可抑制紡紗機內的聚丙烯系樹脂的熱分解,紡紗性或製成長纖維不織布時的拉伸強度提高。The spinning temperature in the present invention is preferably set to be above (melting temperature of raw material resin + 30°C) and below (melting point of raw material resin + 160°C). That is, it can be said that approximately 190°C to 320°C is a preferred range. By setting the spinning temperature preferably above 190°C, the viscosity of the spun molten resin is reduced, which can promote the ultra-fine fiber. In addition, by setting the spinning temperature preferably below 320°C, more preferably below 300°C, the thermal decomposition of the polypropylene resin in the spinning machine can be suppressed, and the spinnability or tensile strength when making a long-fiber non-woven fabric can be improved.

(b)對熔融樹脂實施熔噴法而獲得長纖維不織布的步驟 熔噴法是藉由自具有規定孔徑的熔噴用模口噴出原料而形成纖維,對其噴出部自一定角度噴射熱風,藉此使纖維極細化,使經極細化的纖維堆積於捕集部,藉此形成長纖維不織布的方法。 (b) Step of obtaining a long-fiber nonwoven fabric by melt-blowing the molten resin The melt-blowing method is a method of forming fibers by spraying raw materials from a melt-blowing die having a predetermined aperture, spraying hot air at a certain angle to the spraying portion to extremely refine the fibers, and accumulating the extremely refined fibers in a collecting portion to form a long-fiber nonwoven fabric.

本發明中的模口較佳為具有多個噴出孔。作為噴出孔的形狀,可使用圓形、三角形、四邊形、Y字形等。其中,圓形的噴出孔於紡紗步驟中的步驟穩定性優異,因此較佳。於圓形的噴出孔的情況下,其直徑較佳為0.08 mm~1.0 mm。藉由使噴出孔的直徑較佳為0.08 mm以上、更佳為0.10 mm以上,不易產生孔堵塞,生產性提高。另外,藉由使噴出孔的直徑較佳為1.0 mm以下、更佳為0.70 mm以下、進而佳為0.50 mm以下,模口內部的樹脂的分配性提高,可製造均勻的不織布。The die mouth of the present invention preferably has a plurality of ejection holes. As the shape of the ejection hole, a circular, triangular, quadrilateral, Y-shaped, etc. can be used. Among them, a circular ejection hole is excellent in step stability in the spinning step and is therefore preferred. In the case of a circular ejection hole, the diameter is preferably 0.08 mm to 1.0 mm. By making the diameter of the ejection hole preferably 0.08 mm or more, more preferably 0.10 mm or more, hole clogging is less likely to occur, and productivity is improved. In addition, by making the diameter of the ejection hole preferably 1.0 mm or less, more preferably 0.70 mm or less, and further preferably 0.50 mm or less, the distribution of the resin inside the die mouth is improved, and a uniform nonwoven fabric can be produced.

本發明中的熔融樹脂的單孔噴出量較佳為0.01 g/分鐘以上且0.30 g/分鐘以下。藉由使熔融樹脂的單孔噴出量較佳為0.01 g/分鐘以上、更佳為0.03 g/分鐘以上、進而佳為0.05 g/分鐘以上,不易產生斷紗,可製造均勻的不織布。另外,藉由使熔融樹脂的單孔噴出量較佳為0.30 g/分鐘以下、更佳為0.25 g/分鐘以下、進而佳為0.20 g/分鐘以下,纖維容易極細化,製成空氣過濾器時的捕集效率提高。The single-hole ejection amount of the molten resin in the present invention is preferably 0.01 g/min or more and 0.30 g/min or less. By setting the single-hole ejection amount of the molten resin to preferably 0.01 g/min or more, more preferably 0.03 g/min or more, and further preferably 0.05 g/min or more, yarn breakage is less likely to occur, and a uniform nonwoven fabric can be manufactured. In addition, by setting the single-hole ejection amount of the molten resin to preferably 0.30 g/min or less, more preferably 0.25 g/min or less, and further preferably 0.20 g/min or less, the fiber is easily extremely refined, and the collection efficiency when it is made into an air filter is improved.

於本發明中,自所述模口至捕集部的距離較佳為3 cm~100 cm。藉由使自模口至捕集部的距離較佳為3 cm以上、更佳為5 cm以上、進而佳為10 cm以上、尤佳為15 cm以上,從而形成拉伸強度高的長纖維不織布。另外,藉由設為較佳為100 cm以下、更佳為80 cm以下、進而佳為50 cm以下,可獲得質地良好且均勻的長纖維不織布。In the present invention, the distance from the die opening to the collecting part is preferably 3 cm to 100 cm. By setting the distance from the die opening to the collecting part to preferably 3 cm or more, more preferably 5 cm or more, further preferably 10 cm or more, and particularly preferably 15 cm or more, a long fiber nonwoven fabric with high tensile strength is formed. In addition, by setting the distance to preferably 100 cm or less, more preferably 80 cm or less, and further preferably 50 cm or less, a long fiber nonwoven fabric with good quality and uniformity can be obtained.

再者,到此為止,對利用熔噴法來製造長纖維不織布的方法進行了記載,當然亦可利用紡黏法來形成長纖維不織布。紡黏法是藉由如下步驟,即利用模口將熔融樹脂紡紗後,進行冷卻固化,將所獲得的紗條延伸,捕集至移動的網上進行纖維網化後,進行熱接著的步驟來製造長纖維不織布的方法。Furthermore, so far, the method of manufacturing long-fiber nonwoven fabrics by meltblowing has been described, but of course, long-fiber nonwoven fabrics can also be formed by spunbonding. The spunbonding method is a method of manufacturing long-fiber nonwoven fabrics by spinning molten resin through a die, cooling and solidifying it, extending the obtained yarn, capturing it on a moving net to form a fiber net, and then performing a heat-bonding step.

於利用紡黏法來製造本發明的長纖維不織布的情況下,較佳為將所使用的模口的噴出孔的直徑設為0.10 mm以上且0.20 mm以下,於單孔噴出量0.01 g/min以上且0.20 g/min以下的條件下進行紡紗。藉由將噴出孔的直徑與單孔噴出量設為所述範圍,容易使纖維極細化。當利用紡黏法來製造時,構成纖維的聚丙烯樹脂的分子配向提高,因此形成撕裂強度優異的長纖維不織布。When the long fiber nonwoven fabric of the present invention is manufactured by the spunbond method, it is preferred to set the diameter of the ejection hole of the die used to be greater than 0.10 mm and less than 0.20 mm, and to perform spinning under the condition of a single hole ejection amount of greater than 0.01 g/min and less than 0.20 g/min. By setting the ejection hole diameter and the single hole ejection amount to the above range, it is easy to make the fiber extremely fine. When the spunbond method is used for manufacturing, the molecular orientation of the polypropylene resin constituting the fiber is improved, thereby forming a long fiber nonwoven fabric with excellent tear strength.

(c)駐極體加工、後加工 於本發明的長纖維不織布的製造方法中,亦較佳為進行駐極體加工。具體而言,例如可使用如下方法等:於使藉由所述步驟而堆積於捕集部的纖維片材接觸於接地電極上的狀態下,使該接地電極與纖維片材一起移動,同時利用非接觸型的施加電極進行高壓施加,連續地進行駐極體加工而獲得長纖維不織布的方法;對所述纖維片材以足以使水浸透至纖維片材內部的壓力噴霧水的噴流或水滴流並進行駐極體化,使正極性與負極性的電荷均勻地混在而獲得長纖維不織布的方法;或者使所述纖維片材於狹縫狀的噴嘴上通過,利用噴嘴抽吸水,藉此使水浸透至纖維片材中,從而獲得均勻地混在有正極性與負極性的電荷的長纖維不織布的方法(液壓充電(hydrocharge)法)。該些方法中,就駐極體化時的捕集性能優異的方面而言,較佳為使用液壓充電法。 (c) Electrode processing and post-processing In the method for manufacturing the long-fiber nonwoven fabric of the present invention, it is also preferred to perform electrode processing. Specifically, for example, the following method can be used: in a state where the fiber sheet accumulated on the collection portion by the above step is in contact with the ground electrode, the ground electrode is moved together with the fiber sheet, and a non-contact type application electrode is used to apply high voltage, and the electrode processing is continuously performed to obtain a long-fiber nonwoven fabric; water is sprayed on the fiber sheet at a pressure sufficient to allow water to penetrate into the fiber sheet. A method of obtaining a long fiber nonwoven fabric by using a jet or water droplet flow to polarize the fiber sheet so that positive and negative charges are evenly mixed; or a method of passing the fiber sheet through a slit-shaped nozzle and using the nozzle to suck water so that the water penetrates into the fiber sheet to obtain a long fiber nonwoven fabric in which positive and negative charges are evenly mixed (hydraulic charging (hydrocharge) method). Among these methods, the hydrocharge method is preferably used in terms of excellent capture performance during polarization.

另外,於本發明的長纖維不織布的製造方法中,亦可結合長纖維不織布的用途來進行抗菌加工或壓褶加工等後加工。In addition, in the manufacturing method of the long-fiber nonwoven fabric of the present invention, post-processing such as antibacterial processing or pleating processing can also be performed in combination with the use of the long-fiber nonwoven fabric.

[積層體] 本發明的長纖維不織布由於具有如上所述的特性,因此可製成具有至少一層長纖維不織布的積層體。特別是,於本發明的長纖維不織布的兩面積層有紡黏不織布的結構(紡黏不織布/本申請案發明的長纖維不織布/紡黏不織布的結構)的積層體適合用作面罩或防護服。以下,對將本發明的長纖維不織布與紡黏不織布積層的方法的較佳態樣進行具體說明。 [Laminate] Since the long-fiber nonwoven fabric of the present invention has the above-mentioned characteristics, a laminate having at least one layer of the long-fiber nonwoven fabric can be produced. In particular, a laminate having a structure in which a spunbond nonwoven fabric is laminated on both sides of the long-fiber nonwoven fabric of the present invention (spunbond nonwoven fabric/long-fiber nonwoven fabric of the present application/spunbond nonwoven fabric structure) is suitable for use as a mask or protective clothing. The following specifically describes a preferred method of laminating the long-fiber nonwoven fabric of the present invention with a spunbond nonwoven fabric.

於將紡黏不織布與本發明的長纖維不織布積層的情況下,可藉由離線來積層(分別製造紡黏不織布與本發明的長纖維不織布,並將該些積層),亦可藉由在形成紡黏不織布後,利用熔噴法直接形成長纖維不織布來積層。When laminating the spunbond nonwoven fabric and the long fiber nonwoven fabric of the present invention, the lamination can be performed offline (the spunbond nonwoven fabric and the long fiber nonwoven fabric of the present invention are manufactured separately and then laminated), or the lamination can be performed by directly forming the long fiber nonwoven fabric by melt-blowing after forming the spunbond nonwoven fabric.

另外,作為將紡黏不織布與本發明的長纖維不織布熱接著的方法,可列舉:藉由上下一對的輥表面分別實施有雕刻(凹凸部)的熱壓花輥、包含一個輥表面平坦(平滑)的輥與另一個輥表面實施有雕刻(凹凸部)的輥的組合的熱壓花輥、及包含上下一對的平坦(平滑)輥的組合的熱壓延輥等各種輥來進行熱接著的方法;或藉由焊頭(horn)的超音波振動而進行熱熔接的超音波接著等方法。其中,就生產性優異,於部分熱接著部賦予強度,且於該部分熱接著部以外的部分(非接著部)可保持不織布才有的肌膚觸感或通氣性的方面而言,較佳的態樣是使用上下一對的輥表面分別實施有雕刻(凹凸部)的熱壓花輥、或者包含一個輥表面平坦(平滑)的輥與另一個輥表面實施有雕刻(凹凸部)的輥的組合的熱壓花輥。In addition, as a method for thermally bonding the spunbond nonwoven fabric and the long-fiber nonwoven fabric of the present invention, there can be listed: a method of thermally bonding using various rollers, such as a heat embossing roller having engravings (concave and convex parts) on the surfaces of an upper and lower pair of rollers, a heat embossing roller comprising a combination of a roller having a flat (smooth) surface and a roller having an engraving (concave and convex part) on the surface of the other roller, and a heat embossing roller comprising a combination of an upper and lower pair of flat (smooth) rollers; or an ultrasonic bonding method of thermally melting by ultrasonic vibration of a horn. Among them, in terms of excellent productivity, imparting strength to a portion of the heat-bonded portion, and maintaining the skin-touch or breathability that is unique to non-woven fabrics in the portion other than the heat-bonded portion (non-bonded portion), a better embodiment is to use a heat embossing roller with engravings (concave and convex portions) on the surfaces of an upper and lower pair of rollers, or a heat embossing roller that is a combination of a roller with a flat (smooth) surface and a roller with an engraving (concave and convex portion) on the surface of the other roller.

作為熱壓花輥的表面材質,為了獲得由充分的熱接著帶來的效果,且防止一個壓花輥的雕刻(凹凸部)轉印至另一個輥表面,較佳為金屬製。As the surface material of the heat embossing roller, in order to obtain the effect brought by sufficient heat bonding and prevent the engraving (convex and concave parts) of one embossing roller from being transferred to the surface of another roller, it is preferably made of metal.

由此種熱壓花輥造成的壓花接著面積率較佳為3%以上且30%以下。藉由使壓花接著面積率較佳為3%以上、更佳為5%以上、進而佳為8%以上,作為積層不織布可獲得能供於實用的拉伸強度、撕裂強度、耐起毛等機械特性。另一方面,藉由使壓花接著面積率較佳為30%以下、更佳為25%以下、進而佳為20%以下,可確保通氣性。即便於使用超音波接著等接著方法的情況下,壓花接著面積率亦較佳為相同的範圍。The embossing bonding area ratio by such a hot embossing roller is preferably 3% or more and 30% or less. By making the embossing bonding area ratio preferably 3% or more, more preferably 5% or more, and further preferably 8% or more, mechanical properties such as tensile strength, tear strength, and pilling resistance that can be used practically can be obtained as a laminated nonwoven fabric. On the other hand, by making the embossing bonding area ratio preferably 30% or less, more preferably 25% or less, and further preferably 20% or less, air permeability can be ensured. Even when using a bonding method such as ultrasonic bonding, the embossing bonding area ratio is preferably in the same range.

所謂此處所述的壓花接著面積率,是指熱接著部於積層不織布整體中所佔的比例,具體而言,於藉由一對具有凹凸的輥來進行熱接著的情況下,是指上側輥的凸部與下側輥的凸部重疊並抵接於不織布層的部分(熱接著部)於積層不織布整體中所佔的比例。另外,於藉由具有凹凸的輥與平坦輥來進行熱接著的情況下,是指具有凹凸的輥的凸部抵接於不織布層的部分(熱接著部)於積層不織布整體中所佔的比例。進而,於進行超音波接著的情況下,是指藉由超音波加工來進行熱熔著的部分(熱接著部)於積層不織布整體中所佔的比例。The so-called embossing bonding area ratio mentioned here refers to the ratio of the heat-bonded part to the whole laminated nonwoven fabric. Specifically, when heat bonding is performed by a pair of rollers with concave and convex shapes, it refers to the ratio of the part where the convex part of the upper roller overlaps with the convex part of the lower roller and abuts against the nonwoven fabric layer (heat-bonded part) to the whole laminated nonwoven fabric. In addition, when heat bonding is performed by a roller with concave and convex shapes and a flat roller, it refers to the ratio of the part where the convex part of the roller with concave and convex shapes abuts against the nonwoven fabric layer (heat-bonded part) to the whole laminated nonwoven fabric. Furthermore, in the case of ultrasonic bonding, it refers to the proportion of the portion that is thermally fused by ultrasonic processing (thermal bonding portion) in the entire laminated nonwoven fabric.

作為由熱壓花輥或超音波接著造成的熱接著部的形狀,可使用圓形、橢圓形、正方形、長方形、平行四邊形、菱形、正六邊形及正八邊形等。另外,熱接著部較佳為於積層不織布的長度方向(搬送方向)與寬度方向上分別以一定間隔均勻地存在。藉此,可減低積層不織布的強度的偏差。As the shape of the heat-bonded portion formed by heat embossing rolls or ultrasonic bonding, a circle, an ellipse, a square, a rectangle, a parallelogram, a rhombus, a regular hexagon, a regular octagon, etc. can be used. In addition, the heat-bonded portion is preferably evenly present at a certain interval in the length direction (conveying direction) and the width direction of the laminated nonwoven fabric. Thereby, the variation in the strength of the laminated nonwoven fabric can be reduced.

熱接著時的熱壓花輥的表面溫度較佳為設為(所使用的聚丙烯系樹脂的熔點-50℃)以上且(所使用的聚丙烯系樹脂的熔點-15℃)以下。藉由將熱壓花輥的表面溫度的下限設為相對於所使用的聚丙烯系樹脂的熔點而較佳為-50℃以上、相對於所使用的聚丙烯系樹脂的熔點而更佳為-45℃以上,可獲得能供於實用的拉伸強度、撕裂強度、耐起毛等機械特性的積層不織布。另外,藉由將熱壓花輥的表面溫度的上限設為相對於所使用的聚丙烯系樹脂的熔點而較佳為-15℃以下、相對於所使用的聚丙烯系樹脂的熔點而更佳為-20℃以下,可抑制過度的熱接著,可獲得通氣性高的積層不織布。The surface temperature of the heat embossing roller during heat bonding is preferably set to be greater than (melting point of the polypropylene resin used - 50°C) and less than (melting point of the polypropylene resin used - 15°C). By setting the lower limit of the surface temperature of the heat embossing roller to preferably be greater than -50°C relative to the melting point of the polypropylene resin used, and more preferably greater than -45°C relative to the melting point of the polypropylene resin used, a laminated nonwoven fabric having mechanical properties such as tensile strength, tear strength, and pilling resistance that can be used in practical applications can be obtained. In addition, by setting the upper limit of the surface temperature of the heat embossing roller to preferably -15°C or lower relative to the melting point of the polypropylene resin used, and more preferably -20°C or lower relative to the melting point of the polypropylene resin used, excessive heat bonding can be suppressed and a laminated nonwoven fabric with high air permeability can be obtained.

再者,於聚丙烯系樹脂包含兩種以上的原料的情況下,當觀測到兩個以上的熔點時,較佳為調整成相對於所觀測到的熔點中最低的溫度而為所述範圍。Furthermore, when the polypropylene resin contains two or more raw materials and two or more melting points are observed, it is preferred to adjust the temperature to the above range relative to the lowest temperature among the observed melting points.

熱接著時的熱壓花輥的線壓較佳為10 N/cm以上且500 N/cm以下。藉由使輥的線壓較佳為10 N/cm以上、更佳為50 N/cm以上、進而佳為100 N/cm以上、尤佳為150 N/cm以上,可獲得能供於實用的拉伸強度、撕裂強度、耐起毛等機械特性的積層不織布。另一方面,藉由使熱壓花輥的線壓較佳為500 N/cm以下、更佳為400 N/cm以下、進而佳為300 N/cm以下,可獲得通氣性或柔軟性優異的積層不織布。The linear pressure of the heat embossing roller during heat bonding is preferably 10 N/cm or more and 500 N/cm or less. By setting the linear pressure of the roller preferably 10 N/cm or more, more preferably 50 N/cm or more, further preferably 100 N/cm or more, and particularly preferably 150 N/cm or more, a laminated nonwoven fabric having mechanical properties such as tensile strength, tear strength, and pilling resistance that can be used in practical applications can be obtained. On the other hand, by setting the linear pressure of the heat embossing roller preferably 500 N/cm or less, more preferably 400 N/cm or less, and further preferably 300 N/cm or less, a laminated nonwoven fabric having excellent air permeability or softness can be obtained.

另外,於本發明中,以調整積層不織布的厚度為目的,於利用所述熱壓花輥進行熱接著之前及/或之後,可藉由包含上下一對的平坦輥的熱壓延輥來實施熱壓接。所謂上下一對的平坦輥,是指輥的表面無凹凸的金屬製輥或彈性輥,可藉由使金屬製輥與金屬製輥成對,或使金屬製輥與彈性輥成對來構成。In addition, in the present invention, for the purpose of adjusting the thickness of the laminated nonwoven fabric, before and/or after the heat bonding using the heat embossing pattern roller, heat embossing can be performed by heat embossing rollers including a pair of upper and lower flat rollers. The so-called upper and lower pair of flat rollers refers to a metal roller or elastic roller with no unevenness on the roller surface, and can be configured by pairing a metal roller with a metal roller, or a metal roller with an elastic roller.

再者,所謂本發明中的彈性輥,是指與金屬製輥相比較包含具有高彈性的材質的輥,例如可列舉由紙、棉及芳香族聚醯胺紙等製作的紙輥;或由胺基甲酸酯系樹脂、環氧系樹脂、矽系樹脂、聚酯系樹脂及硬質橡膠及該些的混合物製作的樹脂製的輥等。Furthermore, the so-called elastic roller in the present invention refers to a roller made of a material having higher elasticity than a metal roller, for example, a paper roller made of paper, cotton, and aromatic polyamide paper, or a roller made of a resin made of urethane resin, epoxy resin, silicone resin, polyester resin, hard rubber, and a mixture thereof.

可對本發明的積層體賦予功能性藥劑。作為功能性藥劑,可列舉親水劑、撥水劑、撥油劑、抗靜電劑、抗菌劑、抗病毒劑、防臭劑、芳香劑、冷感劑等,但並無特別限定。Functional agents can be added to the laminate of the present invention. Examples of functional agents include hydrophilic agents, water repellent agents, oil repellent agents, antistatic agents, antibacterial agents, antiviral agents, deodorants, fragrances, cooling agents, etc., but are not particularly limited.

賦予功能性藥劑的方法並無特別限定,例如可使用含浸、噴霧、接觸輥等。The method of applying the functional agent is not particularly limited, and for example, impregnation, spraying, contact roller, etc. can be used.

[過濾器、防護服、面罩] 本發明的長纖維不織布可廣泛用於過濾器、醫療衛生材料、生活材料及工業材料等,由於粒子的捕集效率與通氣性此兩者優異,因此可特別適合用於空氣過濾器等過濾器用途、或面罩等衛生材料及防塵用或抗病毒用的防護服。 [實施例] [Filters, protective clothing, masks] The long-fiber nonwoven fabric of the present invention can be widely used in filters, medical and sanitary materials, living materials, industrial materials, etc. Due to its excellent particle capture efficiency and air permeability, it is particularly suitable for use in filters such as air filters, sanitary materials such as masks, and protective clothing for dust or antiviral use. [Examples]

其次,基於實施例對本發明進行詳細說明。但是,本發明並不僅限定於該些實施例。再者,於各物性的測定中無特別記載者是基於所述方法來進行測定。Next, the present invention is described in detail based on the embodiments. However, the present invention is not limited to these embodiments. Furthermore, in the measurement of various physical properties, those not particularly described are measured based on the above methods.

[測定方法] (1)步驟通過性 將於紡紗步驟中無斷紗或於捲取步驟中無片材斷裂且可穩定地獲得不織布的情況設為「可」,將於紡紗步驟中產生斷紗或於捲取步驟中產生片材斷裂而無法穩定地獲得長纖維不織布的情況設為「不可」。 [Measurement method] (1) Step passability If there is no yarn breakage in the spinning step or no sheet breakage in the winding step and a nonwoven fabric can be obtained stably, it is rated as "OK". If there is yarn breakage in the spinning step or sheet breakage in the winding step and a long-fiber nonwoven fabric cannot be obtained stably, it is rated as "NO".

(2)單位面積重量 基於所述JIS L1913:2010「通常不織布試驗方法」的「6.2 每單位面積的質量」進行測定。 (2) Weight per unit area Measured based on "6.2 Mass per unit area" of JIS L1913:2010 "Test methods for normal nonwoven fabrics".

(3)長纖維不織布的零剪切黏度 使用UBM股份有限公司製造的「萊奧索爾(Reosol)G3000」作為流變儀,利用直徑20 mm的平行板如上所述般進行測定。 (3) Zero shear viscosity of long-fiber nonwoven fabrics Using "Reosol G3000" manufactured by UBM Co., Ltd. as a rheometer, the measurement was performed as described above using parallel plates with a diameter of 20 mm.

(4)纖維的平均纖維徑 使用日立高新技術(Hitachi High-technologies)股份有限公司製造的「S-5500」作為掃描式電子顯微鏡,如上所述般進行測定。 (4) Average fiber diameter of fibers Measured as described above using "S-5500" manufactured by Hitachi High-technologies Co., Ltd. as a scanning electron microscope.

(5)長纖維不織布中的有機過氧化物的含量 於超音波處理中使用亞速旺(ASONE)股份有限公司製造的超音波清洗器「VS-100 III」,於PTFE過濾器中使用愛多邦得科(Advantec)東洋股份有限公司製造的「T010A」,於高效液相層析儀(HPLC)中使用島津製作所股份有限公司製造的「LC-20A」,於質譜計(MS)中使用薩依埃克斯(Sciex)製造的「API4000」,於管柱中使用作為ODS系管柱的住化分析中心股份有限公司製造的「薩米帕克斯(SUMIPAX)ODS A系列」,利用所述方法進行測定。 (5) Content of organic peroxides in long-fiber nonwoven fabrics For ultrasonic treatment, an ultrasonic cleaner "VS-100 III" manufactured by ASONE Co., Ltd. was used, for PTFE filter, a "T010A" manufactured by Advantec Toyo Co., Ltd. was used, for high performance liquid chromatography (HPLC), a "LC-20A" manufactured by Shimadzu Corporation was used, for mass spectrometry (MS), a "API4000" manufactured by Sciex, and for ODS columns, a "SUMIPAX ODS A Series" manufactured by Sumika Analytical Center Co., Ltd. was used, and the above method was used for measurement.

(6)長纖維不織布的空隙率 使用基恩士(KEYENCE)股份有限公司製造的「VR-3050」作為3D顯微鏡,利用所述方法進行測定。 (6) Porosity of long-fiber nonwoven fabrics The measurement was performed using the VR-3050 manufactured by KEYENCE Corporation as a 3D microscope using the above method.

(7)長纖維不織布的粒子的捕集效率 於不織布的寬度方向上的5處採取縱×橫=15 cm×15 cm的測定用樣品,針對各樣品,使用圖1所示的捕集效率測定裝置測定捕集效率。於該圖1的捕集效率測定裝置中,於設置測定樣品(M)的樣品保持器(1)的上游側連結粉塵收納箱(2),於下游側連結有流量計(3)、流量調整閥(4)及鼓風機(5)。另外,可於樣品保持器(1)上使用粒子計數器(6),經由切換旋塞(7)分別測定測定樣品(M)的上游側的粉塵個數與下游側的粉塵個數。 (7) Particle collection efficiency of long-fiber nonwoven fabric Measurement samples with a length × width = 15 cm × 15 cm were collected at 5 locations in the width direction of the nonwoven fabric, and the collection efficiency of each sample was measured using the collection efficiency measurement device shown in Figure 1. In the collection efficiency measurement device of Figure 1, a dust collection box (2) is connected to the upstream side of a sample holder (1) in which a measurement sample (M) is set, and a flow meter (3), a flow regulating valve (4) and a blower (5) are connected to the downstream side. In addition, a particle counter (6) can be used on the sample holder (1) to measure the number of dust particles on the upstream side and the number of dust particles on the downstream side of the measurement sample (M) by switching the valve (7).

於測定捕集效率時,利用蒸餾水將聚苯乙烯0.309U 10%溶液(半井(Nacalai Tesque)股份有限公司製造)稀釋至200倍,填充於粉塵收納箱(2)中。其次,將測定樣品(M)設置於樣品保持器(1),以過濾器通過速度成為6.5 m/分鐘的方式利用流量調整閥(4)調整風量,使粉塵濃度於1萬個/(2.83×10 -4m 3)以上且4萬個/(2.83×10 -4m 3)以下的範圍(2.83×10 -4m 3與0.01 ft 3相等)的範圍內穩定,針對每1個測定樣品,利用粒子計數器(6)(理音(RION)股份有限公司製造、「KC-01D」)將測定樣品(M)的上游的粉塵個數(D)及下游的粉塵個數(d)測定3次,依據JIS K0901:1991「氣體中的粉塵試樣捕集用過濾材的形狀、尺寸以及性能試驗方法」的「5.2 捕集率試驗」,並使用下述計算式來求出0.3 μm~0.5 μm的粒子的捕集效率(%)。將3個測定樣品的平均值作為最終的捕集效率。 捕集效率(%)=〔1-(d/D)〕×100 (其中,d表示下游粉塵的3次測定總個數,D表示上游粉塵的3次測定總個數) When measuring the capture efficiency, a polystyrene 0.309U 10% solution (manufactured by Nacalai Tesque Co., Ltd.) was diluted 200 times with distilled water and filled into the dust collection box (2). Next, the measurement sample (M) is placed in the sample holder (1), and the air volume is adjusted using the flow control valve (4) so that the filter passing speed becomes 6.5 m/min, so that the dust concentration is stabilized within the range of 10,000 particles/(2.83 ×10-4 m3 ) or more and 40,000 particles/(2.83× 10-4 m3 ) or less (2.83× 10-4 m3 is equivalent to 0.01 ft3 ). For each measurement sample, the number of dust particles (D) upstream and the number of dust particles (d) downstream of the measurement sample (M) are measured three times using a particle counter (6) (manufactured by RION Co., Ltd., "KC-01D"), according to JIS K0901:1991 "Test Methods for Shape, Size and Performance of Filter Materials for Collecting Dust in Gases""5.2 Collection Efficiency Test", and use the following formula to calculate the collection efficiency (%) for particles of 0.3 μm to 0.5 μm. The average value of the three measured samples is taken as the final collection efficiency. Collection efficiency (%) = [1- (d/D)] × 100 (where d represents the total number of downstream dust measured three times, and D represents the total number of upstream dust measured three times)

(8)長纖維不織布的通氣度 使用泰斯克測試(TEXTEST)股份有限公司製造的通氣性評價裝置「FX3340」,基於JIS L1096:2010「梭織物及針織物的布料試驗方法」的「8.26 通氣性」中記載的「A法(弗雷澤(Fragile)形法)」進行測定。 (8) Air permeability of long-fiber nonwoven fabrics The air permeability evaluation device "FX3340" manufactured by TEXTEST Co., Ltd. was used to perform the measurement based on the "A method (Fragile method)" described in "8.26 Air permeability" of JIS L1096:2010 "Test methods for fabrics of woven and knitted fabrics".

[聚丙烯系樹脂] 於實施例1~實施例5及比較例1~比較例5中,用作原料樹脂的聚丙烯系樹脂如下所述。 ‧聚丙烯樹脂A(於表1中表述為PP-A):利安德巴塞爾(lyondellbasell)公司製造的「HP461X」(商品名) ‧聚丙烯樹脂B(於表1中表述為PP-B):利安德巴塞爾(lyondellbasell)公司製造的「MF650Y」(商品名) ‧聚丙烯樹脂C(於表1中表述為PP-C):利安德巴塞爾(lyondellbasell)公司製造的「HP461Y」(商品名) ‧聚丙烯樹脂D(於表1中表述為PP-D):普瑞曼聚合物(Prime Polymer)股份有限公司製造的「S10CL」(商品名) ‧聚丙烯樹脂E(於表1中表述為PP-E):桑阿羅馬(Sun-aroma)股份有限公司製造的「VS200A」(商品名) ‧聚丙烯樹脂F(於表1中表述為PP-F):利安德巴塞爾(lyondellbasell)公司製造的「HP5036」(商品名) ‧有機過氧化物母料α(於表1中表述為MB-α):寶利德(Polytechs)公司製造的「VMPP10X」(商品名)(2,5-二甲基-2,5-二(第三丁基過氧化)己烷的含有率為10質量%的聚丙烯樹脂)。 [Polypropylene resin] In Examples 1 to 5 and Comparative Examples 1 to 5, the polypropylene resin used as the raw material resin is as follows. ‧Polypropylene resin A (described as PP-A in Table 1): "HP461X" (trade name) manufactured by LyondellBasell ‧Polypropylene resin B (described as PP-B in Table 1): "MF650Y" (trade name) manufactured by LyondellBasell ‧Polypropylene resin C (described as PP-C in Table 1): "HP461Y" (trade name) manufactured by LyondellBasell ‧Polypropylene resin D (described as PP-D in Table 1): "S10CL" (trade name) manufactured by Prime Polymer Co., Ltd. ‧Polypropylene resin E (described as PP-E in Table 1): "VS200A" (trade name) manufactured by Sun-aroma Co., Ltd. ‧Polypropylene resin F (expressed as PP-F in Table 1): "HP5036" (trade name) manufactured by LyondellBasell ‧Organic peroxide masterbatch α (expressed as MB-α in Table 1): "VMPP10X" (trade name) manufactured by Polytechs (polypropylene resin containing 10% by mass of 2,5-dimethyl-2,5-di(tert-butylperoxy)hexane).

[實施例1] 將聚丙烯樹脂A與有機過氧化物母料α以聚丙烯樹脂A:有機過氧化物母料α=97.5:2.5的質量比乾式摻合,獲得摻合碎片。於將摻合碎片整體的質量設為100質量%時,有機過氧化物於該摻合碎片(原料樹脂組成物)中所佔的比例、即原料樹脂組成物中的有機過氧化物的添加量為0.25質量%。將該摻合碎片投入至200℃的用以向紡紗機中供給原料的擠出機中,使聚丙烯樹脂A與有機過氧化物反應,同時獲得熔融樹脂。 [Example 1] Polypropylene resin A and organic peroxide masterbatch α are dry-blended at a mass ratio of polypropylene resin A: organic peroxide masterbatch α = 97.5:2.5 to obtain blended fragments. When the mass of the entire blended fragments is set to 100 mass%, the proportion of organic peroxide in the blended fragments (raw material resin composition), that is, the amount of organic peroxide added to the raw material resin composition, is 0.25 mass%. The blended fragments are placed in an extruder for supplying raw materials to a spinning machine at 200°C, and the polypropylene resin A and the organic peroxide react to obtain a molten resin.

將所獲得的熔融樹脂直接供給至直徑0.12 mm的噴出孔配置於一直線上的模口,藉由熔噴法而於單孔噴出量0.05 g/min、模口溫度280℃、熱風壓0.16 MPa的條件下進行紡紗,利用設置於距噴出孔為20 cm的下方的輸送機捕集纖維,利用捲取機呈卷狀捲取,藉此獲得長纖維不織布。The obtained molten resin was directly supplied to a die with ejection holes of 0.12 mm in diameter arranged in a straight line, and spinning was performed by melt blowing under the conditions of single hole ejection amount of 0.05 g/min, die temperature of 280°C, and hot air pressure of 0.16 MPa. The fibers were collected by a conveyor arranged 20 cm below the ejection hole and rolled up by a winder to obtain a long fiber nonwoven fabric.

將所獲得的長纖維不織布的評價結果示於表1中。The evaluation results of the obtained long fiber nonwoven fabric are shown in Table 1.

[實施例2] 將聚丙烯樹脂A與有機過氧化物母料α設為聚丙烯樹脂A∶有機過氧化物母料α=95.0:5.0的質量比,除此以外,藉由與實施例1相同的方法而獲得長纖維不織布。 [Example 2] A long-fiber nonwoven fabric was obtained by the same method as Example 1 except that the mass ratio of polypropylene resin A to organic peroxide masterbatch α was set to polypropylene resin A: organic peroxide masterbatch α = 95.0:5.0.

將所獲得的長纖維不織布的評價結果示於表1中。The evaluation results of the obtained long fiber nonwoven fabric are shown in Table 1.

[實施例3] 將聚丙烯樹脂A與有機過氧化物母料α設為聚丙烯樹脂A∶有機過氧化物母料α=92.5:7.5的質量比,除此以外,藉由與實施例1相同的方法而獲得長纖維不織布。 [Example 3] A long-fiber nonwoven fabric was obtained by the same method as Example 1 except that the mass ratio of polypropylene resin A to organic peroxide masterbatch α was set to polypropylene resin A: organic peroxide masterbatch α = 92.5:7.5.

將所獲得的長纖維不織布的評價結果示於表1中。The evaluation results of the obtained long fiber nonwoven fabric are shown in Table 1.

[實施例4] 將聚丙烯樹脂B與有機過氧化物母料α設為聚丙烯樹脂B:有機過氧化物母料α=99.0:1.0的質量比,除此以外,藉由與實施例1相同的方法而獲得長纖維不織布。 [Example 4] A long-fiber nonwoven fabric was obtained by the same method as Example 1 except that the mass ratio of polypropylene resin B and organic peroxide masterbatch α was set to polypropylene resin B: organic peroxide masterbatch α = 99.0:1.0.

[實施例5] 將聚丙烯樹脂C與有機過氧化物母料α設為聚丙烯樹脂C:有機過氧化物母料α=97.5:2.5的質量比,除此以外,藉由與實施例1相同的方法而獲得長纖維不織布。 [Example 5] A long-fiber nonwoven fabric was obtained by the same method as Example 1 except that the mass ratio of polypropylene resin C and organic peroxide masterbatch α was set to polypropylene resin C: organic peroxide masterbatch α = 97.5:2.5.

將所獲得的長纖維不織布的評價結果示於表1中。The evaluation results of the obtained long fiber nonwoven fabric are shown in Table 1.

[實施例6] 將聚丙烯樹脂D與有機過氧化物母料α設為聚丙烯樹脂D:有機過氧化物母料α=92.5:7.5的質量比,除此以外,藉由與實施例1相同的方法而獲得長纖維不織布。 [Example 6] A long-fiber nonwoven fabric was obtained by the same method as Example 1 except that the mass ratio of polypropylene resin D and organic peroxide masterbatch α was set to polypropylene resin D: organic peroxide masterbatch α = 92.5:7.5.

將所獲得的長纖維不織布的評價結果示於表1中。The evaluation results of the obtained long fiber nonwoven fabric are shown in Table 1.

[表1] [表1] 實施例1 實施例2 實施例3 實施例4 實施例5 實施例6 原料樹脂 聚丙烯樹脂[1] PP-A PP-A PP-A PP-B PP-C PP-D 有機過氧化物母料[2] MB-α MB-α MB-α MB-α MB-α MB-α 所述[1]與[2]的混合比(質量比例、 [1]:[2]) 97.5:2.5 95.0:5.0 92.5:7.5 99.0:1.0 97.5:2.5 92.5:7.5 有機過氧化物的添加量[質量%] 0.25 0.50 0.75 0.10 0.25 0.75 步驟通過性 纖維 平均纖維徑[μm] 0.48 0.42 0.38 0.45 0.46 0.41 長纖維不織布 190℃的零剪切黏度[Pa·s] 8.3 6.0 5.4 8.8 7.6 5.7 有機過氧化物的含量[ppm] 166 210 253 89 180 241 Mw 69000 57000 53000 71000 62000 55000 Mw/Mn 3.39 3.13 2.96 2.18 3.61 2.88 單位面積重量[g/m 2] 20 20 20 20 20 20 空隙率[%] 93.3 93.1 92.7 91.9 93.4 92.9 粒子的捕集效率[%] 68 62 63 70 64 66 通氣度[cm 3/(cm 2·s)] 35.3 34.4 32.7 26.1 32.2 31.6 [Table 1] [Table 1] Embodiment 1 Embodiment 2 Embodiment 3 Embodiment 4 Embodiment 5 Embodiment 6 Raw material resin Polypropylene resin[1] PP-A PP-A PP-A PP-B PP-C PP-D Organic peroxide masterbatch[2] MB-α MB-α MB-α MB-α MB-α MB-α The mixing ratio of [1] and [2] (mass ratio, [1]: [2]) 97.5:2.5 95.0:5.0 92.5:7.5 99.0:1.0 97.5:2.5 92.5:7.5 Addition amount of organic peroxide [mass %] 0.25 0.50 0.75 0.10 0.25 0.75 Step Pass Can Can Can Can Can Can Fiber Average fiber diameter [μm] 0.48 0.42 0.38 0.45 0.46 0.41 Long fiber nonwoven fabric Zero shear viscosity at 190℃ [Pa·s] 8.3 6.0 5.4 8.8 7.6 5.7 Content of organic peroxides [ppm] 166 210 253 89 180 241 M 69000 57000 53000 71000 62000 55000 Mw/Mn 3.39 3.13 2.96 2.18 3.61 2.88 Weight per unit area [g/m 2 ] 20 20 20 20 20 20 Void ratio [%] 93.3 93.1 92.7 91.9 93.4 92.9 Particle collection efficiency [%] 68 62 63 70 64 66 Air permeability [cm 3 / (cm 2 ·s)] 35.3 34.4 32.7 26.1 32.2 31.6

[比較例1] 將聚丙烯樹脂A與有機過氧化物母料α設為聚丙烯樹脂A∶有機過氧化物母料α=99.0:1.0的質量比,除此以外,藉由與實施例1相同的方法而獲得長纖維不織布。[Comparative Example 1] A long-fiber nonwoven fabric was obtained by the same method as in Example 1 except that the mass ratio of the polypropylene resin A to the organic peroxide masterbatch α was set to polypropylene resin A:organic peroxide masterbatch α=99.0:1.0.

將所獲得的長纖維不織布的評價結果示於表2中。The evaluation results of the obtained long fiber nonwoven fabric are shown in Table 2.

[比較例2] 將聚丙烯樹脂A與有機過氧化物母料α設為聚丙烯樹脂A:有機過氧化物母料α=87.5:12.5的質量比,除此以外,欲藉由與實施例1相同的方法而獲得長纖維不織布,但由於強度小且於捲取步驟中片材斷裂,因此無法獲得長纖維不織布。 [Comparative Example 2] The mass ratio of polypropylene resin A and organic peroxide masterbatch α was set to polypropylene resin A: organic peroxide masterbatch α = 87.5:12.5. In addition, a long-fiber nonwoven fabric was obtained by the same method as in Example 1. However, due to the low strength and the sheet breaking during the winding step, the long-fiber nonwoven fabric could not be obtained.

針對已斷裂的片材的斷片,分別測定零剪切黏度與有機過氧化物的含量,將結果示於表2中。The zero shear viscosity and the content of organic peroxide were measured for the broken pieces of the sheet, and the results are shown in Table 2.

[比較例3] 僅將聚丙烯樹脂B投入至260℃的擠出機中並供給至齒輪泵,除此以外,藉由與實施例1相同的方法而獲得長纖維不織布。 [Comparative Example 3] A long-fiber nonwoven fabric was obtained by the same method as in Example 1 except that the polypropylene resin B was fed into an extruder at 260°C and supplied to a gear pump.

將所獲得的長纖維不織布的評價結果示於表2中。The evaluation results of the obtained long fiber nonwoven fabric are shown in Table 2.

[比較例4] 將聚丙烯樹脂E與有機過氧化物母料α設為聚丙烯樹脂E∶有機過氧化物母料α=90.0:10.0的質量比,除此以外,藉由與實施例1相同的方法而獲得長纖維不織布。除此以外,藉由與實施例1相同的方法而獲得長纖維不織布。 [Comparative Example 4] A long-fiber nonwoven fabric was obtained by the same method as in Example 1 except that the mass ratio of polypropylene resin E to organic peroxide masterbatch α was set to polypropylene resin E: organic peroxide masterbatch α = 90.0:10.0. A long-fiber nonwoven fabric was obtained by the same method as in Example 1 except that the mass ratio of polypropylene resin E to organic peroxide masterbatch α was set to 90.0:10.0.

將所獲得的長纖維不織布的評價結果示於表2中。The evaluation results of the obtained long fiber nonwoven fabric are shown in Table 2.

[比較例5] 將聚丙烯樹脂F與有機過氧化物母料α設為聚丙烯樹脂F∶有機過氧化物母料α=92.5:7.5的質量比,除此以外,藉由與實施例1相同的方法而獲得長纖維不織布。 [Comparative Example 5] A long-fiber nonwoven fabric was obtained by the same method as in Example 1 except that the mass ratio of polypropylene resin F to organic peroxide masterbatch α was set to polypropylene resin F: organic peroxide masterbatch α = 92.5:7.5.

將所獲得的長纖維不織布的評價結果示於表2中。The evaluation results of the obtained long fiber nonwoven fabric are shown in Table 2.

[表2] [表2] 比較例1 比較例2 比較例3 比較例4 比較例5 原料樹脂 聚丙烯樹脂[1] PP-A PP-A PP-B PP-E PP-F 有機過氧化物母料[2] MB-α MB-α - MB-α MB-α 所述[1]與[2]的混合比(質量比例、 [1]:[2]) 99.0:1.0 87.5:12.5 (100:0) 90.0:10.0 92.5:7.5 有機過氧化物的添加量[質量%] 0.10 1.25 0 1.00 0.75 步驟通過性 不可 纖維 平均纖維徑[μm] 0.68 - 0.62 1.42 1.38 長纖維不織布 190℃的零剪切黏度[Pa·s] 11.7 4.2 12.0 19.1 18.6 有機過氧化物的含量[ppm] 98 368 0 296 229 Mw 75000 40000 76000 82000 80000 Mw/Mn 3.89 2.79 2.35 2.62 2.89 單位面積重量[g/m 2] 20 - 20 20 20 空隙率[%] 91.1 - 89.6 90.3 89.1 粒子的捕集效率[%] 61 - 65 61 64 通氣度[cm 3/(cm 2·s)] 15.6 - 12.6 20.2 18.8 [Table 2] [Table 2] Comparison Example 1 Comparison Example 2 Comparison Example 3 Comparison Example 4 Comparison Example 5 Raw material resin Polypropylene resin[1] PP-A PP-A PP-B PP-E PP-F Organic peroxide masterbatch[2] MB-α MB-α - MB-α MB-α The mixing ratio of [1] and [2] (mass ratio, [1]: [2]) 99.0:1.0 87.5:12.5 (100:0) 90.0:10.0 92.5:7.5 Addition amount of organic peroxide [mass %] 0.10 1.25 0 1.00 0.75 Step Pass Can No Can Can Can Fiber Average fiber diameter [μm] 0.68 - 0.62 1.42 1.38 Long fiber nonwoven fabric Zero shear viscosity at 190℃ [Pa·s] 11.7 4.2 12.0 19.1 18.6 Content of organic peroxides [ppm] 98 368 0 296 229 M 75000 40000 76000 82000 80000 Mw/Mn 3.89 2.79 2.35 2.62 2.89 Weight per unit area [g/m 2 ] 20 - 20 20 20 Void ratio [%] 91.1 - 89.6 90.3 89.1 Particle collection efficiency [%] 61 - 65 61 64 Air permeability [cm 3 / (cm 2 ·s)] 15.6 - 12.6 20.2 18.8

實施例1~實施例6中記載的不織布的粒子的捕集效率與通氣性此兩者優異。相對於此,比較例中,獲得了不織布的比較例1、比較例3、比較例4、比較例5中記載的不織布雖然粒子的捕集效率與實施例1~實施例6中記載的不織布同等,但是通氣性變差。另外,於比較例2中,於捲取步驟中片材會斷裂,而無法獲得不織布。The nonwoven fabrics described in Examples 1 to 6 were excellent in both particle collection efficiency and air permeability. In contrast, among the comparative examples, the nonwoven fabrics described in Comparative Examples 1, 3, 4, and 5, which obtained nonwoven fabrics, had particle collection efficiency equivalent to that of the nonwoven fabrics described in Examples 1 to 6, but had poor air permeability. In Comparative Example 2, the sheet broke during the winding step, and the nonwoven fabric could not be obtained.

1:樣品保持器 2:粉塵收納箱 3:流量計 4:流量調整閥 5:鼓風機 6:粒子計數器 7:切換旋塞 M:測定樣品 1: Sample holder 2: Dust collection box 3: Flow meter 4: Flow regulating valve 5: Blower 6: Particle counter 7: Switching cock M: Measurement sample

圖1是例示本發明的長纖維不織布的粒子的捕集效率的測定所涉及的捕集效率測定裝置並加以說明的剖面概念圖。FIG. 1 is a cross-sectional conceptual diagram for illustrating and explaining a collection efficiency measuring device for measuring the particle collection efficiency of a long-fiber nonwoven fabric of the present invention.

1:樣品保持器 1: Sample holder

2:粉塵收納箱 2: Dust collection box

3:流量計 3: Flow meter

4:流量調整閥 4: Flow regulating valve

5:鼓風機 5: Blower

6:粒子計數器 6: Particle counter

7:切換旋塞 7: Switch the cock

M:測定樣品 M:Measurement sample

Claims (12)

一種長纖維不織布,包括包含聚丙烯系樹脂的纖維,且所述長纖維不織布中,所述纖維的平均纖維徑為0.05 μm以上且5.00 μm以下,所述長纖維不織布於190℃的零剪切黏度為5 Pa·s以上且10 Pa·s以下。A long fiber nonwoven fabric includes fibers containing a polypropylene resin, wherein the average fiber diameter of the fibers in the long fiber nonwoven fabric is greater than or equal to 0.05 μm and less than or equal to 5.00 μm, and the zero shear viscosity of the long fiber nonwoven fabric at 190° C. is greater than or equal to 5 Pa·s and less than or equal to 10 Pa·s. 如請求項1所述的長纖維不織布,其中,所述長纖維不織布含有100 ppm以上且1000 ppm以下的具有以下的通式(1)或通式(2)所表示的結構的有機過氧化物; 此處,R 1~R 3、R 5~R 7為碳原子數1~10的烷基、烯基、苯基、苄基或苯甲醯基,R 4、R 8為碳原子數1~20且除碳原子以外僅包含氫原子的結構。 The long-fiber nonwoven fabric according to claim 1, wherein the long-fiber nonwoven fabric contains 100 ppm or more and 1000 ppm or less of an organic peroxide having a structure represented by the following general formula (1) or general formula (2); Here, R 1 to R 3 and R 5 to R 7 are alkyl, alkenyl, phenyl, benzyl or benzoyl groups having 1 to 10 carbon atoms, and R 4 and R 8 are structures having 1 to 20 carbon atoms and containing only hydrogen atoms other than carbon atoms. 如請求項1或2所述的長纖維不織布,其中,藉由凝膠滲透層析法而求出的所述聚丙烯系樹脂的分子量分佈Mw/Mn為2.00以上且4.00以下。The long fiber nonwoven fabric according to claim 1 or 2, wherein the molecular weight distribution Mw/Mn of the polypropylene resin determined by gel permeation chromatography is 2.00 or more and 4.00 or less. 如請求項1或2所述的長纖維不織布,其中,所述長纖維不織布的空隙率為92.5%以上且99.0%以下。The long fiber nonwoven fabric according to claim 1 or 2, wherein the porosity of the long fiber nonwoven fabric is 92.5% or more and 99.0% or less. 一種積層體,具有至少一層包含如請求項1或2所述的長纖維不織布的層。A laminate having at least one layer comprising the long-fiber nonwoven fabric as described in claim 1 or 2. 一種過濾器,使用如請求項1或2所述的長纖維不織布。A filter using the long-fiber nonwoven fabric as claimed in claim 1 or 2. 一種防護服,使用如請求項1或2所述的長纖維不織布。A protective clothing using the long-fiber nonwoven fabric as described in claim 1 or 2. 一種面罩,使用如請求項1或2所述的長纖維不織布。A face mask using the long-fiber nonwoven fabric as described in claim 1 or 2. 一種長纖維不織布的製造方法,將於溶體流動速率為500 g/10分鐘以上且2000 g/10分鐘以下的聚丙烯系樹脂中添加具有以下的通式(1)或通式(2)所表示的結構的有機過氧化物而得的原料樹脂組成物熔融而獲得熔融樹脂,對所述熔融樹脂實施熔噴法而獲得長纖維不織布; 此處,R 1~R 3、R 5~R 7為碳原子數1~10的烷基、烯基、苯基、苄基或苯甲醯基,R 4、R 8為碳原子數1~20且除碳原子以外僅包含氫原子的結構。 A method for producing a long-fiber nonwoven fabric comprises: melting a raw material resin composition obtained by adding an organic peroxide having a structure represented by the following general formula (1) or (2) to a polypropylene resin having a melt flow rate of 500 g/10 minutes or more and 2000 g/10 minutes or less to obtain a molten resin; and subjecting the molten resin to a melt-blowing method to obtain a long-fiber nonwoven fabric; Here, R 1 to R 3 and R 5 to R 7 are alkyl, alkenyl, phenyl, benzyl or benzoyl groups having 1 to 10 carbon atoms, and R 4 and R 8 are structures having 1 to 20 carbon atoms and containing only hydrogen atoms other than carbon atoms. 如請求項9所述的長纖維不織布的製造方法,其中,藉由如下方式而獲得所述熔融樹脂:使所述聚丙烯系樹脂與所述有機過氧化物於用以向實施所述熔噴法的紡紗機中供給原料的擠出機內反應。The method for producing a long-fiber nonwoven fabric as described in claim 9, wherein the molten resin is obtained by reacting the polypropylene-based resin with the organic peroxide in an extruder for supplying raw materials to a spinning machine for performing the melt-blowing method. 如請求項9或10所述的長纖維不織布的製造方法,其中,將所述有機過氧化物以混練聚丙烯系樹脂與有機過氧化物而得的母料的形態添加。The method for producing a long-fiber nonwoven fabric according to claim 9 or 10, wherein the organic peroxide is added in the form of a masterbatch obtained by kneading a polypropylene-based resin and the organic peroxide. 如請求項9或10所述的長纖維不織布的製造方法,其中,所述原料樹脂組成物中的所述有機過氧化物的添加量為0.2質量%以上且1.0質量%以下。The method for producing a long-fiber nonwoven fabric according to claim 9 or 10, wherein the amount of the organic peroxide added to the raw resin composition is 0.2 mass % or more and 1.0 mass % or less.
TW112133772A 2022-09-22 2023-09-06 Long fiber nonwoven fabric and manufacturing method thereof, and laminate, filter, protective clothing, and face mask TW202413760A (en)

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