TWI251537B - Sheet for leaching - Google Patents
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- TWI251537B TWI251537B TW091135439A TW91135439A TWI251537B TW I251537 B TWI251537 B TW I251537B TW 091135439 A TW091135439 A TW 091135439A TW 91135439 A TW91135439 A TW 91135439A TW I251537 B TWI251537 B TW I251537B
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1251537 ⑴ 玖、發明說明 (發明說明應敘明:發明所屬之技術領域、先前技術、内容、實施方式及圖式簡單說明) 技術領域 本發明係關於紅茶、咖啡、綠茶、中藥等浸出性原料的 抽出所使用之浸出用片材。 先前技術 紅茶、咖啡、綠茶、中藥等浸出性原料的抽出所使用之 浸出用片材要求良好的抽出液浸出性,此外,以茶包形態 所使用的浸出用片材須具有製袋性,亦即,使用熱封口機 須可容易地製袋。 於是,先前,浸出用片材,係使用纖維本身的吸水性低 、浸出性高的合成纖維製不織布。另外,適用於製袋加工 之浸出用片材(大紀商事株式會社製,全紗(FULL VEIL)), 係層積高融點聚酯纖維所構成的紡黏不織布,與低融點聚 酯纖維所構成的梳毛不織布。利用層積此高融點的紡黏不 織布與低融點的梳毛不織布之浸出用片材,將低融點的梳 毛不織布置於内側,重疊兩張浸出用片材,並使用熱封口 機,於熱封口機的加熱頭不融解附著纖維,可容易地熱封 口 〇 但是,利用層積先前的紡黏不織布與梳毛不織布之浸出 用片材,因梳毛不織布的纖維朝梳毛機所定之特定方向配 1251537 (2) 向,無法以不規則方向均勻分散,所以不織布的空隙之孔‘ 徑分布將廣範圍分布。因此,為得到理想的通液速度而調 整浸出用片材之黏格時,將有浸出性原料的微粉末通過浸 出用片材之情形,此外,為完全防止浸出性原料的微粉末 通過’將有通液速度極為低下之問題。 另外,對於茶包周邊部封口寬度從先前的5 mm左右縮小 至2mm左右之近年的市場所需,利用層積先前的纺黏不織 籲 布與梳毛不織布之浸出用片材縮小封口寬度時,因擔任封 口功能的梳毛不織布纖維朝特定方向配向,無法以不規則 万向均勻分散,所以於封口部亦有產生封口強度低的部分 之問題。 對於此般問題,本發明,係於具製袋性的浸出用片材, 即使為縮小封口寬度之情形,使其於封口部不產生封口強 度低的部刀,此外,其目的在於浸出性原料抽出時,一方鲁 面保持理想的通液速度,一方面防止浸出性原料的微粉末 通過。 發明之揭示 本發明者,發現於層積高融點不織布與低融點不織布之 尽出用片材,低融點不織布以乾式不規則分散堆積短纖維 、 相互熱黏接此些父點構成時,因短纖維朝不規則方向均 · 的任何部分,可用同樣的強度 句分散,所以即使於不織布 1251537 Ο) 丨錢^!^ 進行熱封口,另外,因不織布空隙的孔徑分布集中於極為 狹窄的範圍,所以對於所需求的孔徑將不存在過大孔徑的 空隙,於浸出性原料抽出時,可防止浸出性原料的微粉末 通過。 亦即,本發明,係提供一種浸出用片材,其特徵在於浸 出用片材,其層積至少一部分為高融點樹脂的合成纖維, 形成黏格5〜30 g/m2的長纖維不織布,及 至少一部分為低融點樹脂的合成纖維,形成黏格3〜15 g/m2的短纖維不織布, 短纖維不織布,係以乾式不規則地分散堆積纖維長3〜 15 mm的纖維,相互熱黏接所形成, 在浸出用片材的空隙之孔徑與其分布率之關係所示孔 徑分布圖中,最大峰值之分布率係為其他峰值分布率的10 倍以上。 圖式之簡要說明 圖1為本發明之浸出用片材的剖面圖。 圖2為顯示空袋不織布(a)與梳毛不織布(b)的纖維配向 狀態之照片。 圖3為封口強度測試方法之說明圖。 圖4為實施例一的浸出用片材空隙之孔徑分布圖。 圖5為比較例一的浸出用片材空隙之孔徑分布圖。 -9- 1251537 (4) 丨健_蘇 圖6為比較例二的浸出用片材空隙之孔徑分布圖。 圖7為實施例二的浸出用片材空隙之孔徑分布圖。 圖8為實施例二的浸出用片材空隙之孔徑分布圖。 圖9為實施例二的浸出用片材空隙之孔徑分布圖。 圖10為實施例二的浸出用片材空隙之孔徑分布圖。 發明之最佳實施形態 以下,一面參閱圖面一面詳細說明本發明。 圖1為本發明的一種樣態之浸出用片材1,具有長纖維不 織布2與短纖維不織布3之層積構造。 其中,長纖維不織布,其至少一部分為高融點樹脂的合 成纖維,理想為至少一部分由融點170°C以上的高融點樹 脂之合成纖維所形成。藉此,將短纖維不織布置於内側, 重疊兩張浸出用片材,並使用熱封口機之情形,於熱封口 機的加熱頭可防止纖維融解附著。 於此,所謂至少一部分由融點170°C以上的高融點樹脂 之合成纖維形成長纖維不織布,形成長纖維不織布之合成 纖維,其包含只由融點170°C以上的合成樹脂所構成之情 形;由融點170°C以上的合成樹脂構成纖維與融點未滿170 °C的合成樹脂構成纖維之混合纖維的情形;至少表層(鞘) 由融點170°C以上的合成樹脂構成芯鞘構造的纖維之情形 -10-1251537 (1) 发明, the description of the invention (the description of the invention should be described: the technical field, the prior art, the content, the embodiment and the schematic description of the invention) TECHNICAL FIELD The present invention relates to leaching raw materials such as black tea, coffee, green tea, and traditional Chinese medicine. The leaching sheet used was taken out. The leaching sheet used for the extraction of the leaching raw materials such as black tea, coffee, green tea, and traditional Chinese medicines requires good leaching property, and the leaching sheet used in the form of a tea bag must have bag-making properties. That is, the use of a heat sealer requires easy bag making. Then, in the prior art, the leaching sheet is made of a synthetic fiber nonwoven fabric having low water absorbing property and high leaching property. In addition, it is suitable for the leaching sheet for bag making (FULL VEIL), a spunbonded nonwoven fabric made of laminated high-melting polyester fibers, and a low-melting polyester fiber. The combed hair is not woven. The sheet for leaching of the high-melting point spunbonded nonwoven fabric and the low-melting combed nonwoven fabric is arranged such that the low-melting comb is not woven on the inner side, the two leaching sheets are overlapped, and a heat sealing machine is used. The heating head of the heat sealing machine does not melt the attached fibers, and can be easily heat-sealed. However, the woven sheets of the prior spunbonded nonwoven fabric and the combed nonwoven fabric are laminated, and the fibers of the comb-non-woven fabric are assigned 1251537 in a specific direction set by the carding machine ( 2) The direction cannot be uniformly dispersed in the irregular direction, so the pore diameter distribution of the non-woven voids will be widely distributed. Therefore, when the viscosity of the sheet for leaching is adjusted to obtain a desired liquid passing speed, the fine powder of the leaching raw material is passed through the sheet for leaching, and further, the fine powder of the leaching material is completely prevented from passing through There is a problem that the flow rate is extremely low. In addition, in the recent market where the width of the sealing portion of the tea bag is reduced from the previous 5 mm to about 2 mm, when the sealing width is reduced by laminating the previously woven non-woven fabric and the woven fabric sheet. Since the comb-non-woven fabrics having the sealing function are aligned in a specific direction and cannot be uniformly dispersed in the irregular direction, there is a problem in that the sealing portion has a portion having a low sealing strength. In order to solve such a problem, the present invention relates to a sheet for leaching which has a bag-like property, and which does not cause a portion having a low sealing strength in the sealing portion even when the width of the sealing is reduced, and the object is a leaching material. At the time of extraction, one of the ramen faces maintains an ideal liquid passing speed, and on the other hand, the fine powder of the leaching raw material is prevented from passing. DISCLOSURE OF THE INVENTION The present inventors have found that when a high-melting point non-woven fabric and a low-melting-point non-woven fabric are laminated, a low-melting point non-woven fabric is formed by dry-discretely dispersing and stacking short fibers and mutually thermally bonding these parent points. Because any part of the short fiber in the irregular direction can be dispersed with the same intensity sentence, even if the non-woven fabric 1251537 Ο) 丨 money ^! ^ for heat sealing, in addition, the pore size distribution of the non-woven fabric is concentrated in extremely narrow Since the range is small, there is no void having an excessively large pore diameter, and when the leaching raw material is taken out, the fine powder of the leaching raw material can be prevented from passing. That is, the present invention provides a sheet for leaching, characterized in that a sheet for leaching is formed by laminating at least a part of a synthetic fiber of a high-melting point resin to form a long-fiber non-woven fabric having a viscosity of 5 to 30 g/m2. And at least a part of the synthetic fiber of the low melting point resin, forming a short fiber non-woven fabric with a viscosity of 3 to 15 g/m2, and a short fiber non-woven fabric, which is a dry-type irregularly dispersed fiber with a fiber length of 3 to 15 mm, which is mutually heat-adhesive. In the pore size distribution map shown by the relationship between the pore diameter of the void of the sheet for leaching and the distribution ratio thereof, the distribution ratio of the maximum peak is 10 times or more of the other peak distribution ratio. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a cross-sectional view showing a sheet for leaching of the present invention. Fig. 2 is a photograph showing the alignment state of the fibers of the empty bag non-woven fabric (a) and the carded nonwoven fabric (b). Fig. 3 is an explanatory view of a sealing strength test method. Fig. 4 is a view showing the pore size distribution of the voids of the sheet for leaching of the first embodiment. Fig. 5 is a view showing the pore size distribution of the voids of the sheet for leaching of Comparative Example 1. -9- 1251537 (4) 丨健_苏 Figure 6 is a pore size distribution diagram of the voids of the leaching sheet of Comparative Example 2. Fig. 7 is a view showing the pore size distribution of the voids of the sheet for leaching of the second embodiment. Fig. 8 is a view showing the pore size distribution of the voids of the sheet for leaching of the second embodiment. Fig. 9 is a view showing the pore size distribution of the voids of the sheet for leaching of the second embodiment. Fig. 10 is a view showing the pore size distribution of the voids of the sheet for leaching of the second embodiment. BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, the present invention will be described in detail with reference to the drawings. Fig. 1 shows a sheet 1 for leaching of the present invention, which has a laminated structure of a long-fiber nonwoven fabric 2 and a short-fiber nonwoven fabric 3. Among them, a long-fiber non-woven fabric, at least a part of which is a synthetic fiber of a high-melting point resin, is preferably formed of at least a part of a synthetic fiber of a high melting point resin having a melting point of 170 ° C or more. Thereby, the short fibers are not woven on the inner side, and the two sheets for leaching are superposed, and in the case of using a heat sealer, the heat head of the heat sealer prevents the fibers from being melted and adhered. Here, at least a part of the synthetic fiber having a high melting point resin having a melting point of 170 ° C or more forms a long fiber non-woven fabric, and a synthetic fiber of a long fiber non-woven fabric is formed, which comprises a synthetic resin having a melting point of only 170 ° C or more. In the case of a synthetic resin composed of a synthetic resin having a melting point of 170 ° C or more and a synthetic resin having a melting point of less than 170 ° C; at least the surface layer (sheath) is composed of a synthetic resin having a melting point of 170 ° C or more. The situation of the fiber of the sheath structure -10-
1251537 (5) 融點170°C以上的合成樹脂,其可列舉出如高融點聚酯( 高融點聚乙晞對苯二甲酸酯:融點 245°C )、聚醯胺(尼龍 66 :融點245°C )、聚苯硫醚(融點290°C )、聚乳酸(融點178 〇C )等。 形成長纖維不織布之合成纖維的纖維徑,從不織布黏格 安定性的觀點,最好為3 μηι以下。1251537 (5) Synthetic resin with a melting point of 170 ° C or higher, which can be exemplified by high melting point polyester (high melting point polyethylene terephthalate: melting point 245 ° C), polyamide (nylon) 66: melting point 245 ° C), polyphenylene sulfide (melting point 290 ° C), polylactic acid (melting point 178 〇 C) and the like. The fiber diameter of the synthetic fiber forming the long-fiber non-woven fabric is preferably 3 μηι or less from the viewpoint of the stability of the nonwoven fabric.
此般合成纖維不織布化之方法,雖亦可用熔噴等,但是 不堵塞格子,從得到高強度的觀點,最好為紡黏。 另外,長纖維不織布的黏格為5〜3 0 g / m2。黏格未滿5 g/m2時,強度不足,反之,超過30 g/m2時,因浸出性或 機械適用性低下,所以並不理想。In the method of non-woven synthetic fibers, melt-blown or the like may be used, but the lattice is not blocked, and from the viewpoint of obtaining high strength, it is preferable to be spun. In addition, the long fiber non-woven fabric has a viscosity of 5 to 30 g / m 2 . When the viscosity is less than 5 g/m2, the strength is insufficient. On the other hand, when the viscosity exceeds 30 g/m2, the leaching property or mechanical applicability is low, which is not preferable.
此外,於本發明的浸出用片材,短纖維不織布,其至少 一部分為低融點樹脂的合成纖維,理想為至少由融點 80 °C以上未滿170°C的低融點樹脂之合成纖維所形成。藉此 ,將短纖維不織布置於内側,重疊兩張浸出用片材,並使 用熱封口機,可容易地熱封口。 於此,所謂至少一部分由融點80°C以上未滿170°C的低 融點樹脂之合成纖維構成短纖維不織布,形成短纖維不織 布之合成纖維,其包含只由融點80°C以上未滿170°C的合 成樹脂所構成之情形;由融點80°C以上未滿170°C的合成 樹脂構成纖維與該融點以外的纖維之混合纖維的情形;至 -11 -Further, in the leaching sheet of the present invention, the short fiber non-woven fabric, at least a part of which is a synthetic fiber of a low melting point resin, is preferably a synthetic fiber of a low melting point resin having at least a melting point of 80 ° C or more and less than 170 ° C. Formed. Thereby, the short fibers are not woven on the inner side, and the two sheets for leaching are superposed, and the heat sealing machine can be used to easily seal the heat. Here, at least a part of the synthetic fiber having a low melting point resin having a melting point of 80° C. or more and less than 170° C. constitutes a short fiber non-woven fabric, and a synthetic fiber of a short fiber non-woven fabric is formed, which comprises only a melting point of 80° C. or more. a case where a synthetic resin having a temperature of 170 ° C is formed; and a synthetic resin having a melting point of 80 ° C or more and less than 170 ° C constitutes a mixed fiber of fibers and fibers other than the melting point; to -11 -
1251537 ⑹1251537 (6)
少表層由融點8(TC以上未滿170°C的合成樹脂構成芯鞘構 造的纖維之情形。即使其中,於長纖維不織布與短纖維不 織布黏合時,從不破壞不織布空隙的觀點,最好使用芯鞘 構造的纖維。此外,從提高長纖維不織布與短纖維不織布 之黏合強度的觀點,形成長纖維不織布的纖維與形成短纖 維不織布的纖維,最好使用同種類的樹脂,特別是,使用 芯鞘構造的纖維之情形,表層(鞘)的樹脂最好使用同種類 的樹脂。 融點80°C以上未滿170°C的合成樹脂,其可列舉出如低 融點聚酯(低融點聚乙烯對苯二甲酸酯:融點100〜160°C ) 、聚乙晞(融點90〜140°C )、聚丙晞(融點160〜168°C )等。The case where the surface layer is composed of a synthetic resin having a melting point of 8 or less (TC above 170 ° C) constitutes a core-sheath structure. Even in the case where the long-fiber non-woven fabric is bonded to the short-fiber non-woven fabric, it is preferable that the non-woven fabric void is not damaged. The fiber of the core-sheath structure is used. Further, from the viewpoint of improving the bonding strength between the long-fiber non-woven fabric and the short-fiber non-woven fabric, the fibers forming the long-fiber non-woven fabric and the fibers forming the short-fiber non-woven fabric are preferably made of the same kind of resin, in particular, In the case of a core-sheathed fiber, it is preferable to use a resin of the same type as the resin of the surface layer (sheath). A synthetic resin having a melting point of 80 ° C or more and less than 170 ° C may be exemplified by a low melting point polyester (low melting) Point polyethylene terephthalate: melting point 100~160 ° C), polyethylene (melting point 90 ~ 140 ° C), polypropylene (melting point 160 ~ 168 ° C) and so on.
另外,芯鞘構造的纖維,其可列舉出如芯/鞘,分別為 高融點聚酯/低融點聚酯、高融點聚酯/聚乙烯、聚丙烯/ 聚乙烯等。 形成短纖維不織布之合成纖維的纖維長為3〜15mm,最 好為5〜7 mm。纖維長太短時將導致不織布的強度低下, 此外,纖維密度變大,則通液速度將變慢。反之,纖維長 太長時,將使纖維難於均勻分散。 形成短纖維不織布之合成纖維的纖維徑,其視浸出性原 料亦關係到所給予的浸出用片材之孔徑分布,例如,浸出 用片材使用於一般的紅茶茶包之情形,最好為0.1〜3.0d( -12- 1251537 l_ ⑺ : 但尼爾),Ο . 5〜2 . Od更佳。纖維徑太細時,不織布的孔徑 變小,通液速度將變慢。反之,纖維徑太粗時,茶葉等浸 出性原料的微粉末通過不織布,抽出液的口感或外觀將變 差。 此般合成纖維不織布化之方法,首先,藉由乾式不規則 地分散堆積纖維形成樑腹,其次,相互熱黏接纖維的交點 。更具體而言,係以空袋法形成樑腹,再以壓花輪、壓延 等熱處理樑腹。 以空袋法所形成的樑腹,纖維將朝不規則方向以均勻的 厚度分散。另外,即使以壓花輪等熱處理此樑腹,亦不損 壞纖維分散的均一性。因此,像這樣所形成的短纖維不織 布,孔徑分布集中於狹窄範圍,如求取孔徑與其分布率( °/〇 )之關係所示孔徑分布圖的話,最大峰值之分布率係為 其他峰值分布率的10倍以上,較佳為,孔徑分布係在不 均一寬度為1〇〇 μηι以下,最好為50μηι以下,具有單一 ♦ 值。此外,於本發明,孔徑分布係以泡點法(JIS Κ3832)測 出。 另外,像這樣所形成的短纖維不織布之孔徑分布,可藉 由調整纖維徑與黏格敏銳地控制。 此外,纖維朝不規則方向分散的不織布,雖亦可藉由濕 式法之抄紙法取得,但從生產性的觀點,最好使用空袋法 1251537 ⑻Further, the fiber of the core-sheath structure may be, for example, a core/sheath, and is a high melting point polyester/low melting point polyester, a high melting point polyester/polyethylene, a polypropylene/polyethylene, or the like. The synthetic fiber forming the short fiber non-woven fabric has a fiber length of 3 to 15 mm, preferably 5 to 7 mm. When the fiber length is too short, the strength of the non-woven fabric is lowered, and in addition, as the fiber density becomes large, the liquid passing speed becomes slow. Conversely, when the fiber length is too long, it will make it difficult to uniformly disperse the fibers. The fiber diameter of the synthetic fiber forming the short fiber non-woven fabric, and the leaching material is also related to the pore size distribution of the sheet for leaching to be applied. For example, the sheet for leaching is used in a general black tea bag, preferably 0.1. ~3.0d( -12- 1251537 l_ (7) : Daniel), Ο . 5~2 . Od is better. When the fiber diameter is too small, the pore diameter of the non-woven fabric becomes small, and the liquid passing speed becomes slow. On the other hand, when the fiber diameter is too large, the fine powder of the leaching raw material such as tea leaves is passed through the nonwoven fabric, and the texture or appearance of the extract liquid is deteriorated. In the method of non-woven synthetic fibers, first, the fibers are dispersed by irregularly dispersing the fibers, and secondly, the intersections of the fibers are thermally bonded to each other. More specifically, the web is formed by an empty bag method, and the web is heat-treated with an embossing wheel, calendering or the like. In the web formed by the empty bag method, the fibers will be dispersed in a uniform thickness in an irregular direction. Further, even if the web is heat-treated by an embossing wheel or the like, the uniformity of fiber dispersion is not impaired. Therefore, in the short fiber non-woven fabric thus formed, the pore size distribution is concentrated in a narrow range, and if the pore size distribution map is obtained by the relationship between the pore diameter and the distribution ratio (°/〇), the distribution ratio of the maximum peak value is other peak distribution ratio. More than 10 times, preferably, the pore size distribution is not less than 1 〇〇μηι, more preferably 50 μηι or less, and has a single ♦ value. Further, in the present invention, the pore size distribution is measured by the bubble point method (JIS Κ 3832). Further, the pore size distribution of the short fiber non-woven fabric thus formed can be sharply controlled by adjusting the fiber diameter and the viscosity. In addition, the non-woven fabric in which the fibers are dispersed in an irregular direction can be obtained by the wet paper method, but from the viewpoint of productivity, it is preferable to use the empty bag method 1251537 (8)
於本發明,長纖維不織布與短纖維不織布之層積方法, 亦可個別形成長纖維不織布與短纖維不織布後,重疊兩者 ,再以壓花輪、壓延等熱處理進行層積。另外,亦可於長 纖維不織布上形成構成短纖維不織布的樑腹,對此再以壓 花輪、壓延等熱處理,同時進行形成短纖維不織布的樑腹 不織布化,及短纖維不織布與長纖維不織布的層積黏合。In the present invention, the method of laminating the long-fiber non-woven fabric and the short-fiber non-woven fabric may be formed by separately forming the long-fiber non-woven fabric and the short-fiber non-woven fabric, and then laminating them by heat treatment such as embossing, rolling, or the like. Further, the web of the short fiber non-woven fabric may be formed on the long-fiber non-woven fabric, and heat-treated by embossing, rolling, or the like, and the web non-woven fabric forming the short-fiber non-woven fabric, and the short-fiber non-woven fabric and the long-fiber non-woven fabric may be simultaneously formed. Lamination bonding.
依照本發明的浸出用片材,層積低融點的短纖維不織布 與高融點的長纖維不織布,短纖維不織布的孔徑分布如上 述係集中於狹窄範圍,另一方面,因長纖維不織布之孔徑 粗大,作為浸出用片材整體之孔徑分布,如求取孔徑與其 分布率(% )之關係所示孔徑分布圖時,最大峰值之分布 率亦為其他峰值分布率的10倍以上,較佳為,孔徑分布 係在不均一寬度為ΙΟΟμιη以下,最好為50μπι以下,具有 單一辛值。於是,確保理想的通液速度,並且於浸出性原 料抽出時,可防止浸出性原料的微粉末通過浸出用片材。 再者,熱封浸出用片材時擔任黏接性的短纖維不織布之低 融點纖維,因朝不規則方向以均勻的厚度分散,所以即使 於不織布的任何部分,皆可用同樣的強度進行熱封口。於 是,即使封口寬度狹窄,於封口部,將不產生封口強度不 足的部分。如上所述,本發明之浸出用片材,係作為形成 -14- 1251537 發明說明續買 (9) 紅茶、咖啡、綠茶、中藥等浸出性原料的茶包,極為有用 之片材。 本發明之浸出用片材,如圖1所示,除了具有長纖維不 織布2與短纖維不織布3之層積構造,視需要亦可層積其 他的織布、不織布等。例如,為了提高長纖維不織布與短 纖維不織布的黏合強度,可於這些之間設置黏合用不織布 實施例 以下,基於實施例具體說明本發明。 測試例一 芯/鞘使用高融點聚乙烯對苯二甲酸酯/低融點聚乙烯 對苯二甲酸酯的芯鞘構造纖維(纖維徑1.0 d、纖維長5mm) ,以空袋法形成樑腹,再施以熱封口製作空袋不織布,另 外,使用同樣的纖維製作梳毛不織布。其次,從各個不織 布切出9.0 cmx6.0 cm的樣本與100 cmx 100 cm的樣本各十個 ,並測量其重量。結果顯示於表1、表2。此外,圖2(a) 顯示空袋不織布的照片,同圖(b)顯示梳毛不織布的照片 -15- 1251537According to the leaching sheet of the present invention, a short fiber non-woven fabric having a low melting point and a long fiber non-woven fabric having a high melting point are laminated, and a pore size distribution of the short fiber non-woven fabric is concentrated in a narrow range as described above, and on the other hand, a long fiber non-woven fabric is used. When the pore diameter is large, as the pore size distribution of the entire sheet for leaching, for example, the pore size distribution map of the relationship between the pore diameter and the distribution ratio (%) is obtained, the distribution ratio of the maximum peak value is also 10 times or more of the other peak distribution ratio, preferably. Therefore, the pore size distribution has a single symplectic value with a non-uniform width of ΙΟΟμιη or less, preferably 50 μm or less. Thus, the desired liquid passing rate is ensured, and when the leaching raw material is taken out, the fine powder of the leaching raw material can be prevented from passing through the leaching sheet. Further, when the sheet for heat-sealing the sheet is heat-sealed, the low-melting point fiber which is a non-woven fabric of the non-woven fabric is dispersed in a uniform thickness in an irregular direction, so that heat can be applied to the same strength even in any part of the non-woven fabric. seal. Therefore, even if the sealing width is narrow, in the sealing portion, a portion having insufficient sealing strength will not be produced. As described above, the sheet for leaching of the present invention is an extremely useful sheet for forming a tea bag which is a leaching material such as black tea, coffee, green tea or Chinese medicine, which is described in the paragraph -14-1251537. As shown in Fig. 1, the leaching sheet of the present invention has a laminated structure of long-fiber nonwoven fabric 2 and short-fiber nonwoven fabric 3, and may be laminated with other woven fabrics, non-woven fabrics or the like as necessary. For example, in order to improve the bonding strength between the long-fiber non-woven fabric and the short-fiber non-woven fabric, a non-woven fabric for bonding may be provided between them. Hereinafter, the present invention will be specifically described based on examples. Test Example One core/sheath using high melting point polyethylene terephthalate / low melting point polyethylene terephthalate core sheath construction fiber (fiber diameter 1.0 d, fiber length 5 mm), with empty bag method The web was formed into a web, and an air bag was used to make an empty bag non-woven fabric. In addition, the same fiber was used to make a comb non-woven fabric. Next, a sample of 9.0 cm x 6.0 cm and ten samples of 100 cm x 100 cm were cut out from each non-woven fabric, and the weight was measured. The results are shown in Tables 1 and 2. In addition, Figure 2(a) shows a photograph of an empty bag non-woven fabric, and Figure (b) shows a photo of a comb non-woven fabric -15- 1251537
do) I發明說明續頁I 表1Do) I invention description Continued page I Table 1
[g / 9.0 cmx6. Ο cm] 樣本 空袋不織布 梳毛不織布 1 0.044 0.056 2 0.045 0.054 3 0.044 0.059 4 0.043 0.057 5 0.044 0.055 6 0.044 0.056 7 0.045 0.059 8 0.044 0.057 9 0.044 0.055 10 0.044 0.058 平均 0.044 0.057 標準偏差 0.00054 0.00162[g / 9.0 cmx6. Ο cm] Sample empty bag non-woven combed wool non-woven fabric 1 0.044 0.056 2 0.045 0.054 3 0.044 0.059 4 0.043 0.057 5 0.044 0.055 6 0.044 0.056 7 0.045 0.059 8 0.044 0.057 9 0.044 0.055 10 0.044 0.058 Average 0.044 0.057 standard deviation 0.00054 0.00162
-16- 1251537 發_明績買 (11) 表2 [g/ lOOcmxlOO cm] 樣本 空袋不織布 梳毛不織布 1 8.14 10.42 2 8.02 10.58 3 8.29 10.32 4 8.23 10. 12 5 8.15 10.71 6 8.31 10.44 7 8.22 10.28 8 8.16 10.41 9 8.07 10.35 10 7.99 10.40 平均 8.16 10.40 標準偏差 0.10245 0.15238 分別於表1、表2,藉由比較空袋不織布與梳毛不織布 的重量之標準偏差,可得知空袋不織布比梳毛不織布,不 織布内黏格的不均一極少。 另外,從圖2,可得知空袋不織布纖維朝不規則方向均 勻分散,而梳毛不織布纖維朝一定方向配向,於黏格不勻 稱。 實施例一、比較例一、比較例二 使用纖維徑 2 · Od的高融點聚酯製作紡黏不織布,其上 17- (12) 1251537 發明說明賴 ^ 使用心/鞘為高融點聚乙埽對#-16- 1251537 发_明绩买(11) Table 2 [g/ lOOcmxlOO cm] Sample empty bag non-woven carded wool non-woven fabric 1 8.14 10.42 2 8.02 10.58 3 8.29 10.32 4 8.23 10. 12 5 8.15 10.71 6 8.31 10.44 7 8.22 10.28 8 8.16 10.41 9 8.07 10.35 10 7.99 10.40 Average 8.16 10.40 Standard deviation 0.10245 0.15238 According to Table 1, Table 2, by comparing the standard deviation of the weight of the empty bag non-woven fabric and the comb non-woven fabric, it can be known that the empty bag non-woven fabric is more woven than the non-woven fabric. There is very little unevenness in the grid. Further, from Fig. 2, it can be seen that the empty bag non-woven fabric fibers are uniformly dispersed in an irregular direction, and the comb-non-woven fabric fibers are aligned in a certain direction, and the adhesiveness is uneven. In the first embodiment, the first comparative example and the second comparative example, the high-melting polyester with a fiber diameter of 2 · Od is used to make a spunbonded non-woven fabric, and the above-mentioned 17-(12) 1251537 invention illustrates that the use of the heart/sheath is a high melting point.埽对#
欲、 卞來二甲I 對苯二甲酸酯的芯鞘構造纖 纖維徑 mm),以空袋法形成樑腹,並 w以蜃花, 點格12g/m2)上製作層積空袋不 員 小練布(黏袼 片材(實施例一)。 另外,使用與形成空袋不織布 、 m 的、_ 度為SI mm),於同上述的紡黏 1 ’布(黏 層積梳毛不織布(黏格8g/m2)之淳山 /又出用片 此外,除了改變壓花輪的壓花形狀外, 製作浸出用片材(比較例二)。 實施例2 除使空袋不織布之黏格為8 g/m2外, 於纺黏不織布上製作層積空袋不織布之^ 評價 (1)封口強度測試 空袋不織布置於内侧,重疊實施例—的 ,熱封口(加熱溫度150°C )寬度15 mm,切 狀(15 mmx50 mm),再由非封口侧撕開的狀 4的剝開載重。第3圖中,符號2,係表示 號3’係表示空袋不織布。 比較例一的浸出用片材,亦同樣置#毛 堯酯/低融點聚乙 2 · Od、纖維長 5 於紡黏不織布( 6g/m2)之浸出用 ^維(但,纖維長 洛12g/m2)上製作 材(比較例一)。 與比較例一同樣 實施例一同樣地 E出用片材。 兩張浸出用片材 出如圖3的短冊 態,計算封口部 紡黏不織布,符 不織布於内側, -18-Desirable, 芯 dimethyl dimethyl terephthalate core sheath structure fiber diameter mm), the empty bag method to form the beam belly, and w 蜃 flower, dot grid 12g / m2) on the laminated empty bag A small woven fabric (adhesive sheet (Example 1). In addition, the use of an empty bag non-woven fabric, m, _ degree is SI mm), in the same as the above-mentioned spunbond 1 'cloth (viscous laminated comb non-woven fabric ( The 淳 / / / / / / / / / / / / / / / / In addition to g/m2, the laminated empty bag non-woven fabric is produced on the spunbonded nonwoven fabric. (1) Sealing strength test The empty bag is not woven on the inner side, and the heat sealing port (heating temperature 150 ° C) is 15 mm wide. , a cut shape (15 mm x 50 mm), and a peeling load of the shape 4 which is torn by the non-sealing side. In Fig. 3, the symbol 2 indicates that the number 3' indicates an empty bag non-woven fabric. Material, also set #毛尧ester / low melting point polyethylene 2 · Od, fiber length 5 in spunbonded non-woven fabric (6g / m2) leaching with ^ Wei (but, The material of the length of 12g/m2) (Comparative Example 1). In the same manner as in the first comparative example 1, the sheet for E was used. The two sheets for leaching were as shown in the short form of Fig. 3, and the sealing portion was calculated. Sticky non-woven fabric, non-woven fabric on the inside, -18-
1251537 (13) 並進行重疊與熱封口,計算該封口部的剝開載重。 結果顯示於表3 表3 [kg/15 mm] 樣本 實施例一 比較例一 1 0.22 0.46 2 0.22 0.68 3 0.23 0.37 4 0.21 0.39 5 0.21 0.41 6 0.22 0.70 7 0.24 0.62 8 0.23 0.33 9 0.20 0.41 10 0.23 0.541251537 (13) and perform overlapping and heat sealing, and calculate the peeling load of the sealing portion. The results are shown in Table 3. Table 3 [kg/15 mm] sample Example 1 Comparative Example 1 0.22 0.46 2 0.22 0.68 3 0.23 0.37 4 0.21 0.39 5 0.21 0.41 6 0.22 0.70 7 0.24 0.62 8 0.23 0.33 9 0.20 0.41 10 0.23 0.54
平均 0.22 0.49 標準偏差 0.01136 0.12778Average 0.22 0.49 standard deviation 0.01136 0.12778
從表3,與比較例一的浸出用片材比較,可得知實施例 一的浸出用片材,其封口強度的不均一極小。 (2) 孔徑分布 使用美國PMI公司製的孔徑分布機(Perm Poro Meter),根 據泡點法(JIS K3832)測量實施例一、實施例二、比較例一 、比較例二的各浸出用片材空隙的孔徑分布。結果顯示於 -19- 1251537From Table 3, as compared with the sheet for leaching of Comparative Example 1, it was found that the sheet for leaching of Example 1 had extremely small unevenness in sealing strength. (2) Pore size distribution Each of the leaching sheets of Example 1, Example 2, Comparative Example 1, and Comparative Example 2 was measured by a bubble point method (JIS K3832) using a pore size distribution machine (Perm Poro Meter) manufactured by PMI Corporation, USA. The pore size distribution of the voids. Showing results in -19- 1251537
第4圖〜第10圖。又,關於實施例二之浸出用片材,測 定其寬方向位置互異之4個地方(第7圖〜第10圖)。 從此些圖,比較例一、比較例二的浸出用片材,其孔徑 分布具有140μηι以上的不均一,且其中具有複數個峰值, 而實施例一的浸出用片材之孔徑分布,ΙΟμηι以下的不均 一之中具有單一峰值,可得知於該處孔徑分布集中。此外 ,實施例2之浸出用片材,於哪個測定點,最大峰值分布 率亦為其他峰值分布率的10倍以上,可得知孔徑分布係 集中於最大奪值。 產業上之利用可能性 如上所述,藉由本發明之浸出用片材,即使是縮小封口 寬度之情形,可顯著降低封口部的封口強度之不均一。另 外,因可敏銳地控制不織布空隙的孔徑分布,較佳為能使 不織布空隙的孔徑分布成單一峰值,所以於浸出性原料抽 出時,一方面可保持理想的通液速度,一方面可防止浸出 性原料微粉末的通過。 -20-Figure 4 ~ Figure 10. Further, regarding the leaching sheet of the second embodiment, four places (Fig. 7 to Fig. 10) in which the positions in the width direction are different from each other were measured. From the above figures, the leaching sheet of Comparative Example 1 and Comparative Example 2 has a pore size distribution having a non-uniformity of 140 μm or more and having a plurality of peaks therein, and the pore size distribution of the leaching sheet of Example 1 is less than or equal to ΙΟμηι. There is a single peak in the heterogeneity, and it can be known that the pore size distribution is concentrated there. Further, at the measurement point of the sheet for leaching of Example 2, the maximum peak distribution ratio was also 10 times or more of the other peak distribution ratio, and it was found that the pore size distribution was concentrated on the maximum value. Industrial Applicability As described above, according to the sheet for leaching of the present invention, even when the width of the seal is reduced, the unevenness of the seal strength of the seal portion can be remarkably reduced. In addition, since the pore size distribution of the non-woven fabric gap can be sharply controlled, it is preferable to make the pore size distribution of the non-woven fabric voids have a single peak value, so that when the leaching raw material is extracted, on the one hand, the ideal liquid passing speed can be maintained, and on the other hand, the leaching can be prevented. The passage of the fine powder of the raw material. -20-
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW091135439A TWI251537B (en) | 2001-12-07 | 2002-12-06 | Sheet for leaching |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/JP2001/010724 WO2003048438A1 (en) | 2001-12-07 | 2001-12-07 | Seeping sheet |
TW91103770 | 2002-03-01 | ||
TW091135439A TWI251537B (en) | 2001-12-07 | 2002-12-06 | Sheet for leaching |
Publications (2)
Publication Number | Publication Date |
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TW200302162A TW200302162A (en) | 2003-08-01 |
TWI251537B true TWI251537B (en) | 2006-03-21 |
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ID=37453695
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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TW091135439A TWI251537B (en) | 2001-12-07 | 2002-12-06 | Sheet for leaching |
Country Status (1)
Country | Link |
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TW (1) | TWI251537B (en) |
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2002
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