[go: up one dir, main page]

TW200300810A - Tissue products having reduced lint and slough - Google Patents

Tissue products having reduced lint and slough Download PDF

Info

Publication number
TW200300810A
TW200300810A TW091134263A TW91134263A TW200300810A TW 200300810 A TW200300810 A TW 200300810A TW 091134263 A TW091134263 A TW 091134263A TW 91134263 A TW91134263 A TW 91134263A TW 200300810 A TW200300810 A TW 200300810A
Authority
TW
Taiwan
Prior art keywords
latex
item
patent application
scope
fabric
Prior art date
Application number
TW091134263A
Other languages
Chinese (zh)
Inventor
Sheng-Hsin Hu
Strong C Chuang
Shan Chen
Kambiz Bayat Makoui
Original Assignee
Kimberly Clark Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Kimberly Clark Co filed Critical Kimberly Clark Co
Publication of TW200300810A publication Critical patent/TW200300810A/en

Links

Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F11/00Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
    • D21F11/14Making cellulose wadding, filter or blotting paper
    • D21F11/145Making cellulose wadding, filter or blotting paper including a through-drying process
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F11/00Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
    • D21F11/02Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines of the Fourdrinier type
    • D21F11/04Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines of the Fourdrinier type paper or board consisting on two or more layers
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21FPAPER-MAKING MACHINES; METHODS OF PRODUCING PAPER THEREON
    • D21F11/00Processes for making continuous lengths of paper, or of cardboard, or of wet web for fibre board production, on paper-making machines
    • D21F11/14Making cellulose wadding, filter or blotting paper
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H23/00Processes or apparatus for adding material to the pulp or to the paper
    • D21H23/76Processes or apparatus for adding material to the pulp or to the paper characterised by choice of auxiliary compounds which are added separately from at least one other compound, e.g. to improve the incorporation of the latter or to obtain an enhanced combined effect
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/33Synthetic macromolecular compounds
    • D21H17/34Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
    • D21H17/35Polyalkenes, e.g. polystyrene
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H21/00Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/14Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
    • D21H21/18Reinforcing agents
    • D21H21/20Wet strength agents
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H21/00Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
    • D21H21/14Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
    • D21H21/22Agents rendering paper porous, absorbent or bulky

Landscapes

  • Paper (AREA)

Abstract

A method for forming a tissue product that is soft and produces relatively low levels of lint and slough is provided. The method includes providing a liquid furnish of cellulosic fibers and forming a multi-layered wet web therefrom. At least one latex having a glass transition temperature less than about 30 DEG C is applied to the furnish , wet web, or combinations thereof in an amount less than about 60 pounds per ton of the dry weight of the cellulosic fibers. The web is then dried such that at least one outer layer of the dried web contains the latex-treated cellulosic fibers.

Description

200300810 玖、發明說明 (發邏趣敘明·翻所屬之技術領域、先前技術,容、實施方式及圖式簡單說明) 【發明所屬之技術領域】 薄紙製品,如面紙,紙巾,浴廁用紙,衛生餐巾紙及其 他相似產品’都會被設計成同時擁有數種重要性質。例如, 這類產品應該具有良好的膨鬆度,柔軟觸感,且應該具有良 好強度 '然而,不幸地,當實施了增加產品某種性質的手段 時’產品的其他特性通常會產生不良影響。 【先前技術】 舉例來説,在造紙程序期間,一般會使用多種樹脂來增 加織物的濕強度。例如,常會使用陽離子樹脂,因爲它們被 ^爲可以較輕易地與陰離子價的纖維素纖維形成鍵結。此 外,天性爲陰性的樹脂也會被用到。例如,Meisei,等人 所發表的美國專利第3844880號就描述了陰離子苯乙烯-丁 一埽乳膠藉著留置幫助而與陰離子纖維素纖維黏結。 雖然強度樹脂可增加織物的強度,它們也容易讓織物變 更而/肖費者通¥不吾歡硬的織物。因此,常使用多種方法 來抵銷這類堅硬並軟化此產品。舉例來説,可利用化學去键 結劑來減少纖維鍵結,藉以增加柔軟度。 儘管如此,減少纖維與化學去鍵結劑的鍵結有時會不良 地影響薄紙製品的強度。例如,相鄰纖維之間的氫鍵會被這 類化學去鍵結劑,以及造紙程序中的機械力破壞。所以,這 類去鍵結劑會產生鬆散键結的纖維,使得纖維從薄紙製品表 面延伸出去。在製造及/或使用期間,這些鍵結鬆散的纖維讦 以從薄紙製品除去,藉以產生棉絨,其被界定成個别之空中200300810 发明 Description of the invention (Description of the technical field, prior art, description, implementation, and drawings of the logo), [Technical field to which the invention belongs] Tissue products, such as facial tissue, paper towels, and toilet paper , Sanitary napkins and other similar products will be designed to have several important properties at the same time. For example, this type of product should have good bulk, be soft to the touch, and have good strength. 'However, unfortunately, when a means to increase a product's properties is implemented,' other characteristics of the product often have an adverse effect. [Prior Art] For example, during the papermaking process, various resins are generally used to increase the wet strength of a fabric. For example, cationic resins are often used because they are easier to form bonds with anionic valence cellulose fibers. In addition, resins that are negative in nature are also used. For example, U.S. Patent No. 3,844,880, issued by Meisei, et al., Describes that anionic styrene-butadiene latex is bound to anionic cellulose fibers by retention. Although strength resins can increase the strength of fabrics, they can also easily change fabrics. As a result, multiple methods are often used to offset this type of hardness and soften the product. For example, chemical debonding agents can be used to reduce fiber bonding and thereby increase softness. Nevertheless, reducing the bonding of fibers to chemical debonding agents sometimes adversely affects the strength of tissue products. For example, hydrogen bonds between adjacent fibers can be disrupted by such chemical debonding agents and mechanical forces in papermaking processes. Therefore, this type of debonding agent will produce loosely bonded fibers, allowing the fibers to extend from the surface of the tissue product. During manufacturing and / or use, these loosely bonded fibers 讦 are removed from tissue paper products, thereby producing lint, which is defined as individual airspace

0續次頁 ΡΚΟΟ 1 -08 1 8-B (發明說明頁不敷使用時, cky- 20030220 -February 20, 2003 請註記並使用續頁) 7 200300810 發明說明$賣胃 飄散的纖維及纖維碎片。再者,造紙程序亦可產生數區彼此 微弱地連結在一起,但相鄰區之間不連結的纖維。結果,在 使用期間,特定的剪切力可以將微弱連結的區域從其他纖維 上解開,藉以產生脱落,即表面(如皮膚或織品)上的纖維束 或小丸。如此之下,使用此類去键結劑常會產生使用時較弱 的、°氏類製品’而產生較多量的棉織和脱洛。 故此,目前需要一種強健,柔軟且只有少量棉絨和脱落 的薄紙製品。 【内容】 根據本發明之一實施例,提供了一種形成薄紙製品的方 法。此方法包括提供纖維素纖維的液體原料,並從此纖維素 纖維的液體原料形成一多層濕織物。至少一乳膠(非離子或陰 離子性)被加到原料,濕織物(如藉喷灑),或它們的組合物 t ’其添加量爲每噸的纖維素纖維乾重60磅,在某些實施 例中,介於每噸纖維素纖維乾重1至40磅,而在某些實施 例中’添加量介於每噸纖維素纖維乾重i至2〇镑。此乳膠 的玻璃過渡溫度少於30,而在某些實施例中大於—25°C。 例如,在某些實施例中,玻璃過渡溫度介於-15。〇至15〇c, 而在某些實施例中介於-10¾至0艺。乳膠可選自苯乙烯-丁 二烯共聚物,聚乙烯基醋酸鹽同相聚合物,乙烯基-醋酸鹽乙 烯共聚物’乙烯基-醋酸鹽丙烯酸共聚物,乙烯-乙埽基氣化 物共聚物,乙埽-乙烯基、氣化物-乙稀基、醋酸鹽三聚合物, 丙烯酸聚乙烯基氯化物聚合物,丙烯酸聚合物以及亞硝酸共 聚物。 [2續次頁(發明說明頁不敷使用時,請註記並使用續苜) PK〇〇i.〇8l8-Becky-20030220 -February 20, 2003 〆、 200300810 ' 發明說明_胃 去鍵〜劑亦可力σ到原料,濕織物或它們的組合物中。去 键結劑的添加細I人 > 、〜1 ’丨於母噸纖維素纖維1至30磅。在某些 貫施例中,士被纟士七丨 、 、、w 可包含一咪峻υ林四級化合物及/或醋類 官能基四級銨化合物。 右4壬的活,濃強度劑亦可加入原料,濕織物或它們的 組合物中。你1丨nn i 使用時,暫時濕強度劑的總添加量可爲每 頓纖維素纖維乾重…"。再者,使用時,濕強度劑的 總添:量可爲每嘴纖維素纖維乾重i至2〇镑。 然後’可以乾燥濕織物,使得最終的乾燥織物具有至少 -經乳膠處理之纖維㈣維的外層。 本發明的其他特色和方面將在下面有更詳細的討論説 明。 【圖式簡單説明】 、本發明將對熟於此項技術者作完整揭示(包栝最佳模 式)’其在本説明書的其餘部份將有更詳細的描述,包括參考 的附加圖式。 第一圖爲可用在本發明造紙程序中之一實施例的概要流 程圖。 第一圖爲可用在本發明造紙程序中之一實施例的概要流 程圖。 第二圖爲可用在本發明造紙程序中之另一實施例的概要 流程圖。 第四圖爲一設備範例的概要説明,此設備可用來測量薄紙 製品的脱落程度。 Θ續次頁 P K00 1 -08 I 8-1 請註記鎌臓頁) 9 200300810 發明說明,_胃 的參考標號表示本發明 在本説明書和圖式中重複使用 中相同或類似的元件或特徵。 【實施方式】 現在,將詳細地參考本發 ’疋公犯例將在10 Continuation page ΡΚΟΟ 1 -08 1 8-B (When the invention description page is insufficient, cky- 20030220 -February 20, 2003 Please note and use the continuation page) 7 200300810 Invention description $ Selling stomach Dispersed fibers and fiber fragments. Furthermore, the papermaking process can also produce fibers that are weakly connected to each other but not connected between adjacent areas. As a result, during use, specific shearing forces can release weakly connected areas from other fibers, thereby creating shedding, that is, fiber bundles or pellets on the surface (such as the skin or fabric). As such, the use of such debonding agents often results in weaker ' s products ' when used, and larger amounts of cotton and delloid. Therefore, there is currently a need for a strong, soft tissue product with only a small amount of lint and shedding. [Content] According to one embodiment of the present invention, a method for forming a tissue paper product is provided. The method includes providing a liquid raw material of cellulose fibers and forming a multilayer wet fabric from the liquid raw material of cellulose fibers. At least one latex (non-ionic or anionic) is added to the raw materials, wet fabrics (such as by spraying), or their composition t 'added at an amount of 60 pounds per ton of cellulose fiber dry weight, in some implementations In the example, the dry weight is between 1 and 40 pounds per ton of cellulose fiber, and in some embodiments the amount is between i and 20 pounds per ton of cellulose fiber dry weight. This latex has a glass transition temperature of less than 30 and in some embodiments greater than -25 ° C. For example, in some embodiments, the glass transition temperature is between -15. 0 to 15 ° c, and in some embodiments between −10 ° to 0 °. The latex may be selected from a styrene-butadiene copolymer, a polyvinyl acetate homophase polymer, a vinyl-vinyl acetate copolymer, a 'vinyl-acetate acrylic copolymer, an ethylene-acetamidine gaseous copolymer, Acetyl-vinyl, gaseous-ethylene, acetate terpolymers, acrylic polyvinyl chloride polymers, acrylic polymers, and nitrous acid copolymers. [2 Continued pages (if the invention description page is insufficient, please note and use the continued alfalfa) PK〇〇i.〇8l8-Becky-20030220 -February 20, 2003 〆, 200300810 Can force σ to raw materials, wet fabrics or combinations thereof. The debonding agent is added in a fine amount of >, ~ 1 ', to 1 to 30 pounds of the mother ton of cellulose fiber. In some embodiments, the sterilizer VII,,, and w may include a quaternary quaternary compound and / or a vinegar functional quaternary ammonium compound. You can also add active, strong strength agents to raw materials, wet fabrics, or combinations thereof. When you use it, the total amount of temporary wet strength agent can be the dry weight of cellulose fiber per day ... ". Furthermore, when used, the total strength of the wet strength agent may be from i to 20 pounds of dry weight of cellulose fiber per mouth. The wet fabric can then be dried so that the final dry fabric has an outer layer of at least-latex-treated fiber dimensions. Other features and aspects of the invention are discussed in more detail below. [Brief description of the drawings] The present invention will fully disclose those skilled in the art (including the best mode), which will be described in more detail in the rest of this specification, including referenced additional drawings . The first diagram is a schematic flowchart of one embodiment that can be used in the papermaking process of the present invention. The first diagram is a schematic flowchart of one embodiment that can be used in the papermaking process of the present invention. The second figure is a schematic flowchart of another embodiment which can be used in the papermaking process of the present invention. The fourth figure is a schematic illustration of an example of a device that can be used to measure the degree of shedding of tissue products. Θ Continued page P K00 1 -08 I 8-1 Please note the sickle page) 9 200300810 Description of the invention, _ Stomach reference number indicates the same or similar element or feature of the present invention in repeated use in this specification and drawings . [Embodiment] Now, reference will be made in detail to this issue.

面提出。各範例是以解釋發明的方式來提供,但不限制本名 明。事實上,熟於此項技術者很容易根據本發明做出各種^ 正和改變,卻不偏離本發明的精神。例如,在一實施例部俗 中所閣明或描述的特色’可以用在另一實施例中而又產生另 -實施例。因此,本發明應涵蓋此類如同附屬之申請專利系 圍内的修正和改變,以及它們的同等物。 大致上,本發明是針對含有多層紙類織物的薄紙製品, 此多層紙類織物具有至少-由處以乳膠的纖維素纖維所形 成的外層。乳膠可與纖維素纖維形成一彈性連結,使產生於 織物具有彈性,強健,且只會產生.旦 ‘ 曰座生少里的棉絨和脱落。於此 使用之“薄紙製品”通常是指各種紙 、Face raised. Examples are provided by way of explanation of the invention, but do not limit the name. In fact, those skilled in the art can easily make various corrections and changes according to the present invention without departing from the spirit of the present invention. For example, features that are described or described in one embodiment may be used in another embodiment to create another embodiment. Therefore, the present invention should cover such amendments and changes as within the scope of the attached patent application, and their equivalents. Roughly, the present invention is directed to a tissue product comprising a multilayer paper fabric having an outer layer formed of at least-cellulose fibers coated with latex. Latex can form an elastic connection with cellulosic fibers, so that the fabric produced is elastic, strong, and can only produce cotton. Once you ’re done, the cotton linters and sheds. "Tissue paper products" as used herein generally refer to various papers,

、明座卩σ,如面紙,浴崩 用紙,紙巾,餐巾等等。一船而丄 ,^ ’、 般而吕’本發明薄紙製品的基重 少於母平万公尺80公克(gsm),在苹此 J佐乐士實她例中少於每平方 公尺6〇公克,且在某些實施例中介於1〇至6〇轉之間。 :多種材料皆可用來形成薄紙製品的紙類織物。例如, 用來製造薄紙製品的材料可包括 祕將^ ^ J ^括由沣多種紙漿程序(如牛皮 、我桌’亞硫酸鹽紙漿,執機姑 w槔械紙漿寺)所形成的纖維。紙漿纖 、准可匕括軟木纖維,其平均纖 „ , 厂减、准長度根據長度重量平均來説 係大於1mm,具體來說介於 1 ~ k η 、至5mm之間。此類軟木纖維 可匕括(但不限制於此)北方 南方軟木,紅木,紅雪松, 反]續次頁 ΡΚΟΟ 1 -08 1 8- (發明說明頁不敷使用時, Becky-20030220 -February 20, 2〇03 請註記並使用續頁) 10 200300810 、 發明說明,續胃 鐵杉,松樹(即南方松),雲杉 成物等等。適用於本發明之商:“),和这些纖維的組明 σ, such as tissue paper, bath paper, paper towels, napkins, etc. The weight of the thin paper products of the present invention is less than 80 grams per square meter (gsm), which is less than 6 per square meter in this case. Gram, and in some embodiments between 10 and 60 revolutions. : A variety of materials can be used to form tissue paper products. For example, the materials used to make tissue products can include fibers formed by various pulp processes (such as cowhide, our table ’sulphite pulp, and mechanical pulping temples). Pulp fiber and quasi-cork fiber, their average fiber „, factory reduction, quasi-length based on length and weight on average is greater than 1mm, specifically between 1 ~ k η to 5mm. Such softwood fibers can be Dagger (but not limited to this) North and South softwood, mahogany, red cedar, reverse] Continued page ΡΚΟΟ 1 -08 1 8- (When the description page of the invention is insufficient, Becky-20030220 -February 20, 2〇03 Please Note and use continuation page) 10 200300810 、 Instructions of the invention, Hemlockia spiralis, pine (ie southern pine), spruce adult, etc. Applicable to the quotient of the present invention: "), and the combination of these fibers

Kimbedy-CIark㈣咖⑽之商尚可得的紙漿纖維包括 品。 商標爲“ LongIac-19”的產 硬木纖維,如桉屬植物, 楓树’白棒,山揚筌 -- 用。在特定例子十,桉屬植物 、 '、可使 择 ^ M 、准尤其能夠增加織物的柔敍 度。桉屬植物纖維亦可提高亮 *、 物的毛孔…… %加不透明性,且改變織 物的毛“構已增加毛細能力。再者,若期望的 生材料的第二纖維也可使用, ° 如、減維紙漿,其來源包括新聞 用紙,回收的硬紙板,辦公室廢 匕祜新聞 ,^ .. ^ ^ 靨、A I ΰ另外,其他天然纖維 也可使用在本發明中,如 T如呂木大麻,紗百牧草,乳草粗絲’ 麗梨莱等等。此外,在某些例子令,合成纖維亦可被利用。 一些合適的合成纖維可包括(但不限制於此)螺縈纖維,乙婦 乙烯基醇共聚物纖維,聚烯烴纖維,聚酯等等。 如上所述’本發明薄紙製品包含至少—多層紙類織物。 此薄紙製品可爲單央層薄紙製品’其中形成薄紙的織物是分 層的(即具有多層);或一多夹層薄紙製品,其中形成多夹層 薄紙製品的織物本身可爲單一或多層。例如,在一實施例 甲’薄紙製品包含由三層所組成的一央層,其中外層包括桉 屬植物纖維而内曾包括北方軟木牛皮紙纖維。若期望的話, 這些層亦可包括多種纖維的混合物。然而,應瞭解到薄紙製 品可包括任何數量的夾層或層,且可由許多種纖維來製成。 根據本發明’乳膠被用在纖維素纖維辛以減少最終薄紙 製品的棉絨和脱落。於此使用之“乳膠”是指天然狀況下主 0續次頁(發明說明頁不敷使用時,請註記並使用續頁) PKO〇l-0818-Becky-20〇30220 -February 20, 2003 11 200300810 發明說明,¾胃 要主水般i液體系統中,聚合材科的天然或合成膠狀散佈。 適用於本發明之乳膠的玻璃過渡溫度通常少於3使得最 織物的彈I·生本負上不會被限制。再者,乳膠的玻璃過渡溫 度通常大於-25。。,以使乳膠的黏度最小&。例如,在某些實 施例中’用於本發明的乳膠的破璃過渡溫度介於_吨至Μ υ之間,而在某些實施例中則介於_1〇亡至〇艺之間。 使用在本發明的乳膠通常爲非離子性或陰離子性,以幫 助、·氏韻物的應用。例如,某些可用在本發明中的合適乳膠 包括(但不祕此)陰性苯乙埽_丁二埽共聚物,聚乙婦基醋酸 鹽同質聚合物,乙埽基-醋酸鹽乙埽共聚物,乙稀基醋酸鹽丙 缚酸共聚物,乙稀-乙烯基氣化物共聚物,乙稀_乙稀基醋酸 鹽二聚合物,丙烯酸聚乙烯基氣化物共聚物,丙缔酸聚合 物’亞硝酸鹽聚合物,以及任何其他此項技術已知的合適陰 離子謂。上述乳膠的電子價(陰離子或非離子性)可以輕易 地改變,如此項技術巾已㈣,在乳膠㈣備過程中利用一 具有所欲電價的穩㈣。合適的乳膠範例描料斤 等人的美國專利第384侧號,其全部内容於此併入參考之。· 辛纖=:不=:乳膠通常被加在造紙程序“濕端”的纖維 素❹中。於此使用之“濕端”—詞是指造紙程序中,織物 在被乾餘W或乾燥後的任何階段。例如,在某些實施例中乳 =可被加到製製機’傾倒槽’機器槽,清潔儲存槽 _的造紙原料中,或直接加到前㈣等 ,二: 原料製成濕織物後,再加人乳膠。例如,在某些實施例: 乳膠可喷灑或打印至-濕織物表面上。例如,在—實施例Commercially available pulp fiber products from Kimbedy-CIark. Hardwood fibers produced under the trademark "LongIac-19", such as eucalyptus, maple ’white sticks, mountain poplars-used. In the specific example 10, Eucalyptus, ', can make ^ M, especially can increase the softness of the fabric. Eucalyptus fiber can also improve the pores of bright and shiny materials…% plus opacity, and changing the fabric structure of the fabric has increased the capillary capacity. Furthermore, if the second fiber of the desired raw material can be used, such as 1. Reduced-dimensional pulp, its sources include newsprint, recycled cardboard, office waste news, ^ .. ^ ^ AI, AI ΰ In addition, other natural fibers can also be used in the present invention, such as T such as Lümu hemp , Sabai hundred grass, milkweed thick silk, Lililai, etc. In addition, in some examples, synthetic fibers can also be used. Some suitable synthetic fibers can include (but not limited to) snail fiber, B Polyvinyl alcohol copolymer fibers, polyolefin fibers, polyesters, etc. As described above, the tissue paper product of the present invention contains at least-multilayer paper fabrics. The tissue paper product may be a single central layer tissue paper product. Layered (ie, having multiple layers); or a multi-layered tissue paper product in which the fabric forming the multi-layered tissue paper product itself may be single or multiple layers. For example, in an embodiment A 'tissue paper product includes three layers A central layer consisting of eucalyptus fibers and northern softwood kraft fibers. If desired, these layers may also include a mixture of multiple fibers. However, it should be understood that tissue products may include any number of interlayer or Layer, and can be made from many kinds of fibers. According to the present invention, 'latex is used in cellulose fiber to reduce lint and shedding of the final tissue product. The "latex" used here refers to the natural 0th order. Pages (please note and use continuation pages when the invention description page is not enough) PKO〇l-0818-Becky-20〇30220 -February 20, 2003 11 200300810 Description of invention, ¾ The stomach is the main water-like liquid system, polymerization Natural or synthetic colloidal dispersion of materials. The glass transition temperature of the latex suitable for the present invention is usually less than 3 so that the elasticity of the most textile fabrics will not be limited. Furthermore, the glass transition temperature of the latex is usually greater than -25 to minimize the viscosity of the latex & for example, in some embodiments' the glass-breaking transition temperature of the latex used in the present invention is between _ ton and Μ υ, and in some implementations In the example, it is between -10 and 0. The latex used in the present invention is usually nonionic or anionic to help the application of the rhyme. For example, some of the Suitable latexes include (but are not secretive of) negative acetophenone-butadiene copolymers, polyethenyl acetate homopolymers, acetoacetate-acetate copolymers, ethylene acetate propionic acid copolymers Polymers, ethylene-vinyl gaseous copolymers, ethylene-vinyl acetate dipolymers, acrylic polyethylene gaseous copolymers, acrylic acid 'nitrite polymers, and any other Suitable anions are known in the art. The electronic valence (anionic or non-ionic) of the above-mentioned latex can be easily changed. Such a technology has already been used. In the preparation process of latex, a stable price with the desired electricity price is used. An example of a suitable latex is described in U.S. Patent No. 384, et al., The entire contents of which are incorporated herein by reference. · Fibre =: No =: Latex is usually added to the cellulose mat on the "wet end" of the papermaking process. The term "wet end" as used herein refers to any stage in the papermaking process where the fabric is left to dry or after drying. For example, in some embodiments, milk = can be added to the papermaking raw materials of the machine's "dumping tank", cleaning storage tanks, or directly to the front rafter, etc. 2: After the raw materials are made into wet fabric, Add human latex. For example, in some embodiments: latex may be sprayed or printed onto a wet fabric surface. For example, in the embodiment

Ξ續次頁 ΡΚ00 1 -081 8-B 請註記並使用 續頁) 200300810 中,濕織物在通過造紙機器時, 任何位置上。 發明說明,f賣頁 礼膠溶液會被喷灑在織物的 的至=:=:紙程序中的哪個位置,多層紙類織物 被:二Γ 膠的。例如’在-實施例中,乳膠 被併入二層紙類纖維的一 -外表面。薄紙製品外層中的乳二卜:界定出薄紙製品的 生的棉絨及脱落。j的謂可以減少薄紙製品所會產 爲了使用來形成薄紙製品的多層紙類織物的僵硬度達 二取广,可利用許多種不同技術來達成。例如,可添加較少 里的礼膠。㈣㈣施例巾,以纖維材料的乾重爲準,乳膠 的添加量爲每噸60磅(6〇lb/T),在某些實施例中介於i旧丁 至40 lb/ΜΤ之間,而在某些實施例中,介於i績丁至2〇 lb/ΜΤ《間。此外,在_特定層中,乳膠的添加量通常少於 纖維材料乾重白勺3%,在某些實施例則介於0.05%至2%之 間’而在某些實施例中介於〇 〇5%至1%之間。進一步地,在 某些實施例中,乳膠的添加量少於整個薄紙製品乾重的3%, 疒某二貫施例中介於〇 〇 5 %至2 °/〇之間,而在某些實施例中介 於0.05%至1%之間。 進一步地,織物的僵硬度亦可藉著只將紙漿加到織物的 外層中來減少。例如,在一實施例中,以三層的紙類織物而 言’可讓各外層皆包含乳膠,而内層則完全不含乳膠。在另 一貫施例中’三層織物的内層和一外層可大體上不含乳膠。 應瞭解到’當提及“大體上不含”乳膠時,微小量的乳膠是 有可能存在其中的。然而,此小量的乳膠通常是由加在外層ΞContinued on the next page PK00 1 -081 8-B Please note and use (continued) In 200300810, the wet fabric passes through the paper machine at any position. Description of the invention, the f-selling solution will be sprayed on the fabric where: ===: where in the paper program, the multilayer paper fabric is: two Γ glue. For example, in the-embodiment, the latex is incorporated into the outer surface of a two-layer paper fiber. Milk in the outer layer of tissue paper products: defines the raw lint and shedding of tissue paper products. J can reduce the production of tissue paper products. The multi-layered paper fabric used to form tissue paper products has a stiffness of two, which can be achieved by many different technologies. For example, you can add less gift gel. Example towels are based on the dry weight of the fibrous material. The amount of latex added is 60 pounds (60 lb / T) per ton, and in some embodiments it ranges from 1 to 40 lb / MT. In some embodiments, it ranges from 0.1 to 20 lb / MT. In addition, in specific layers, the amount of latex added is usually less than 3% of the dry weight of the fiber material, in some embodiments it is between 0.05% and 2%, and in some embodiments it is between 0.000 and 0.000. Between 5% and 1%. Further, in some embodiments, the amount of latex added is less than 3% of the dry weight of the entire tissue product, which is between 0.05% and 2 ° / 〇 in a certain embodiment, and in some implementations. Examples range between 0.05% and 1%. Further, the stiffness of the fabric can be reduced by adding only pulp to the outer layer of the fabric. For example, in one embodiment, using three layers of paper-based fabrics' allows each outer layer to contain latex, while the inner layer is completely free of latex. In another embodiment, the inner and outer layers of the 'three-layer fabric may be substantially free of latex. It will be appreciated that 'when referring to "substantially free of" latex, it is possible that a small amount of latex is present. However, this small amount of latex is usually added by the outer layer

0續次頁 ρΚΟ〇 1 -08 1 8-B (發明說明頁不敷使用時,請註記並使用續頁) ecky’20030220 -February 20, 2003 13 200300810 發明說明續頁 的乳膠所引起,且大體上不會影響薄紙製品的僵硬度。 若期望的話,乳膠亦可藉著沈澱輔助加到纖維素纖維 中,而幫助乳膠留在纖維上。例如,在纖維素纖維中添加一 “反應組成物”是有用的。反應組成物可以與纖維素纖維上 的陰離子團形成鍵結(即共價,離子鍵結等等)。例如,在一 實她例中,可使用一陽離子組成物,來與纖維上的自由羰基 形成離子鍵結。此類反應組成物可以降低整個纖維的負價, 且在某些實施例中,甚至讓纖維變成正價。所以,當乳膠被 添加到此類已改過電價的纖維中時,乳膠可以較輕易地留在 上面。 大致上,許多種反應組成物皆可被加在纖維素纖維中以 幫助乳膠留置。正常情況下’亦期望此類反應組成物具有額 外的功能,例如能夠增加強度及/或柔軟度。例如,在某些實 施例中’可以添加-濕強度劑來進一步增加薄紙製品的強 度,以及幫助乳膠的留置。於此使用之“濕強度劑”是當加 到纖維素纖維中時,可以讓最終產物或薄片的濕幾何抗張強 度對乾幾何抗張強度的比例超過〇」的物質。通常這些物質 都被稱爲“永久m誠“暫時”㈣度劑。如此項技 術:斤熟知的’暫時和永久濕強度劑某些時候亦有乾強度劑的 功能,以在乾燥時提高薄紙製品的強度。 濕強度劑的添加量可以變化,其絲據所欲的薄紙製品 特性而定。例如’在某些實施例中’濕強度劑加到纖維素纖 維中的總添加量可介於(以纖維材料的乾重爲準)每嘴】邦 ib/τ)至601b/T之間,在某些實施例中介於η·至儿^ 200300810 發明說明$賣;1; 之間’而在某些實施例中介於7 lb/T至13 lb/T之間。濕強 度劑可加到多層紙類織物的任何層中。 合適的永久濕強度劑通常可溶於水,陽離子少或聚合的 樹脂’而可自身交鏈(同質交鏈)或與木質纖維的纖維素或其 他組成物交鏈。此類化合物的範例揭示於美國專利 2345543 ; 29261 16 ;和2926154號,這些内容於此併入參考 之。此類作用劑的其中一類别包括聚胺-環氧氣丙烷,聚氨基 化合物環氧氣丙烷或聚氨基化合物-胺環氧氣丙烷樹脂,共同 稱爲“ PAE樹脂”。這些物質的例子描述於Keim的美國專 利第3700623號以及Keim的3772076號,其内容於此併入 參考之’且這些物質 Hercules,Inc·(位在 Wilmington,Del.) 有販賣’商品名稱爲“ Kymene” ,即Kymene 557H或 557LX。例如,Kymene 557LX是一種聚氨基化合物環氧氯丙 燒聚合物’其包含陽離子基而可與紙漿纖維上的陰離子基形 成離子鍵’還包含了 azetidinium基團,其可與紙蒙纖維上的 羰基形成共價鍵且作用時與聚合物支幹形成交鏈。 其他合適的材料包括基礎活性化的聚氨-環氧氯丙烷樹 脂,其揭示於Petrovich的美國專利編號第3885 號, Petrovich的美國專利編號第3899388號,Petr〇vich的美國專 利編號第4丨29528號,Petrovich的美國專利編號第4147586 號,Van Eanam的美國專利編號第4^29^號,其内容於此 併入參考之。聚乙烯亞胺樹脂亦適用於固定纖維與纖維之間 的鍵結。另一類别的永久型濕強度劑包括氨基樹脂(即尿素_ 甲醛和三聚氰胺-甲醛)。 0續次頁(發明說明頁不敷使用時,請註記並使用續W) PKOO!-08l8-Becky~20030220 -February 20, 2003 〆、 200300810 發明說明,續頁 若使用的話,永久濕強度劑可被加到纖維素纖維中,其 添加量以纖維物質的乾重爲準,爲i lb/T至2〇 lb/T之間, 在某些實施例中介於2 lb/T至1〇丨b/T之間,而在某些實施 例中介於3 lb/T至6 lb/T之間。 暫時濕強度劑亦可用在本發明中,合適的暫時濕強度劑 可選自,此項技術已知的作用劑,如二乙醛澱粉,聚乙烯亞 胺,甘露半乳聚糖膠,乙二醛,和二乙醛甘露半乳聚糖。乙 酸乙埽基氨基化合物濕強度樹脂也是有用的,其在0 Continued page ρΚΟ〇1 -08 1 8-B (When the description page of the invention is insufficient, please note and use the continuation page) ecky'20030220 -February 20, 2003 13 200300810 The description of the invention is caused by the latex and is generally It does not affect the stiffness of tissue products. If desired, latex can also be added to the cellulose fibers by precipitation aid to help the latex stay on the fibers. For example, it is useful to add a "reaction composition" to the cellulose fibers. The reaction composition can form a bond (ie, covalent, ionic bond, etc.) with an anionic group on the cellulose fiber. For example, in one example, a cationic composition can be used to form an ionic bond with a free carbonyl group on the fiber. Such a reaction composition can reduce the negative valence of the entire fiber, and in some embodiments, even make the fiber become positive valence. Therefore, when latex is added to such electricity-modified fiber, the latex can be easily left on it. In general, many reaction compositions can be added to cellulosic fibers to aid in the retention of latex. Under normal circumstances, such a reaction composition is also expected to have additional functions, such as the ability to increase strength and / or softness. For example, in certain embodiments ' -wet strength agents may be added to further increase the strength of tissue paper products, and to aid in the retention of latex. As used herein, a "wet strength agent" is a substance that, when added to cellulose fibers, allows the ratio of wet geometric tensile strength to dry geometric tensile strength of the final product or sheet to exceed 0 ". These substances are often referred to as "permanent" and "temporary" moisturizers. Such a technique: the well-known 'temporary and permanent wet strength agents' sometimes also have the function of dry strength agents to improve tissue paper products when dry. The strength of the wet strength agent can vary, depending on the desired characteristics of the tissue product. For example, in some embodiments, the total amount of wet strength agent added to the cellulose fiber may be between ( Based on the dry weight of the fiber material) per mouth] between ib ib / τ) and 601b / T, in some embodiments between η · to Er ^ 200300810 Invention Description $ Sale; 1; between ' In some embodiments between 7 lb / T and 13 lb / T. Wet strength agents can be added to any layer of multilayer paper fabrics. Suitable permanent wet strength agents are usually soluble in water, less cation or polymerized resins 'It can cross-link itself (homogeneous cross-linking) or with cellulose or other compositions of wood fibers. Examples of such compounds are disclosed in U.S. Patents 2345543; 29261 16; and 2926154, which are incorporated herein by reference. One of these classes of agents includes poly -Epoxy propane, polyamino compound epoxy propane or polyamino compound-amine epoxy propane resin, collectively referred to as "PAE resin". Examples of these materials are described in US Patent No. 3700623 to Keim and No. 3772076 in Keim, which The contents are incorporated herein by reference and these materials are sold by Hercules, Inc. (located in Wilmington, Del.) Under the trade name "Kymene", that is, Kymene 557H or 557LX. For example, Kymene 557LX is a polyamino compound epoxy The chloropropane polymer 'which contains cationic groups and can form an ionic bond with an anionic group on the pulp fiber' also contains an azetidinium group, which can form a covalent bond with a carbonyl group on the paper cover fiber and act with the polymer branch when acting Other suitable materials include base-activated polyurethane-epichlorohydrin resins, which are disclosed in U.S. Patent No. 3885 to Petrovich, U.S. Patent No. 3899388 to Petrovich, and U.S. Patent to Petrovch No. 4 丨 29528, U.S. Patent No. 4147586 to Petrovich, U.S. Patent No. 4 ^ 29 ^ to Van Eanam, in which Herein incorporated by reference. Polyethyleneimine resins are also suitable for fixing fiber-to-fiber bonds. Another type of permanent wet strength agents include amino resins (ie, urea_formaldehyde and melamine-formaldehyde). 0Continued The next page (please note and use when the description page of the invention is not enough, Continue W) PKOO! -08l8-Becky ~ 20030220 -February 20, 2003 2003, 200300810 Invention description, if the continuation page is used, the permanent wet strength agent can be added The cellulose fiber is added in an amount based on the dry weight of the fiber material, between i lb / T and 20 lb / T, and in some embodiments between 2 lb / T and 10 〇b / T Between, and in some embodiments between 3 lb / T and 6 lb / T. Temporary wet strength agents can also be used in the present invention. Suitable temporary wet strength agents can be selected from agents known in the art, such as diacetaldehyde starch, polyethyleneimine, mannan galactan gum, and ethylenediamine. Aldehyde, and diacetaldehyde mannogalactan. Acetate amino compound wet strength resins are also useful.

Darlington等人的美國專利第5466337號有描述,爲了要參 考,其全部内容於此併入之。有用的水溶性樹脂包括聚丙烯 酿胺樹脂,如商標名稱以Parez爲首的商品,Parez 631NC, 其是由 American Cyanamid Company(位在 Stanford,Conn)所 售。Coscia等人的美國專利編號第3556932號和Wiuiams等 人的355 6933號號大致上有描述此類樹脂,爲了參考,其全 4内谷於此併入之。舉例來説,“ parez ”通常包括一聚丙酿 胺·乙二酸聚合物,其含有陽離子半縮醛根而可與纖維素纖維 上的談根或氫氧根形成離子鍵。這些鍵結可增加紙漿纖維織 物的強度。此外,因爲半縮醛基團容易被水解,所以此類樹 脂所提供的濕強度主要是暫時性的。It is described in Darlington et al. U.S. Patent No. 5,466,337, the entire contents of which are incorporated herein by reference. Useful water-soluble resins include polypropylene amine resins such as those sold under the trade name Parez, Parez 631NC, which is sold by the American Cyanamid Company (Stanford, Conn). Coscia et al., U.S. Pat. No. 3,556,932 and Wiuiams et al., No. 355 6933, generally describe such resins, and their entire inner valleys are incorporated herein by reference. For example, "parez" usually includes a polypropylene amine-glyoxylic acid polymer which contains a cationic hemiacetal radical and can form an ionic bond with a cellulose radical or a hydroxide radical on a cellulose fiber. These bonds increase the strength of the pulp fiber fabric. In addition, because hemiacetal groups are easily hydrolyzed, the wet strength provided by such resins is primarily temporary.

Guerro等人的美國專利第4605702號(爲了參考,於此 併入之)亦説明了藉由乙烯基氨聚合物與乙二醛反應,然後將 聚合物以水溶液基本處理所製得之合適的暫時濕強度劑。相 似的樹脂亦描述於Biorkquist等人的美國專利第4603176 號,Sun等人的593 5 3 83號,以及Wendt等人的6017417號, ¥續次頁(發明說明頁不敷使用時,請註記並使用續頁) ^^001-0818-Becky-20030220 -February 20, 2003 16 200300810 發明說明_頁 爲了參考,其全部内容於此併入之。 由製造商所提供的暫時濕強度劑通常是水溶液的形 式,在某些實施例中,其加入纖維素纖維的量(以纖維物質乾 重爲準)爲1 lb/T至60 lb/T之間,而在某些實施例則介於3 lb/T至40 lb/T之間,且在某些實施例中介於4 lb/T至i5 之間。若期望的話,在添加樹脂之前可調整紙漿的pH値。 例如,Parez樹脂在使用時的pH値通常介於4到8之間。 亦可使用一化學去键結劑來軟化織物,並幫助乳膠留置 在織物上。具體來説,化學去键結劑可以減少織物之一或更 多層中的氫鍵量,而產生較柔軟的產品。可根據對於最終薄 紙製品所期望的特性,來變化去鍵結劑的添加量。舉例而 T ’在某些實施例中,去鍵結劑的添加量可爲1 lb/T至3〇 lb/T(以纖維物質的乾重爲準),在某些實施例則介於3 lb/T 至20 lb/T之間,而在某些實施例則介於6 ib/τ至15 lb/T之 間。去鍵結劑可加到多層紙類織物的任何層中。 任何可以加到纖維素纖維且能夠藉著斷裂氫鍵來提高 織物柔軟感的物質通常可以作爲本發明的去鍵結劑。尤其, 如上所述,通常期望去鍵結劑爲正電價,以與纖維素纖維上 的陰離子基團形成離子鍵。某些合適的陽性去鍵結劑包括(但 不限制於此)季銨化合物,imidazolinium化合物, bis-imidazolinium化合物,二季銨化合物,聚季銨化合物, 酯官能基季銨化合物(即四脂肪酸三烷烴酯鹽),磷脂衍生 物,聚二甲基矽氧烷和相關的陽離子及非離子性的矽樹脂化 合物,脂肪和羧酸衍生物,單體和聚糖類衍生物,聚氫氧根 0續次頁(發明說明頁不敷使用時,請註記並使用續頁) PKOOl-0818-Becky-20030220 -February 20, 2003 \ η 200300810 發明說明$賣買; 石炎氫化合物等等。舉例來説,某些合適的去鍵結劑描述於Guerro et al., U.S. Patent No. 4,605,702 (herein incorporated by reference) also describes a suitable temporary prepared by reacting a vinyl ammonia polymer with glyoxal and then basically treating the polymer in an aqueous solution. Wet strength agent. Similar resins are also described in U.S. Patent No. 4,603,176 to Biorkquist et al., 593 5 3 83 to Sun et al., And 6017417 to Wendt et al. (Continued pages) Use continuation page) ^^ 001-0818-Becky-20030220 -February 20, 2003 16 200300810 Description of the invention_page For reference, the entire contents are incorporated herein. The temporary wet strength agent provided by the manufacturer is usually in the form of an aqueous solution. In some embodiments, the amount of cellulose fiber (based on the dry weight of the fiber material) is 1 lb / T to 60 lb / T. And in some embodiments between 3 lb / T and 40 lb / T, and in some embodiments between 4 lb / T and i5. If desired, the pH of the pulp can be adjusted before the resin is added. For example, the pH of Parez resins in use is usually between 4 and 8. A chemical debonding agent can also be used to soften the fabric and help the latex stay on the fabric. Specifically, chemical debonding agents can reduce the amount of hydrogen bonding in one or more layers of the fabric, resulting in a softer product. The amount of debonding agent added can be varied according to the characteristics desired for the final tissue product. For example, T 'In some embodiments, the debonding agent can be added in an amount of 1 lb / T to 30 lb / T (based on the dry weight of the fiber material), in some embodiments it is between 3 lb / T to 20 lb / T, and in some embodiments between 6 ib / τ to 15 lb / T. Debonding agents can be added to any layer of the multilayer paper fabric. Any substance which can be added to cellulose fibers and which can improve the softness of the fabric by breaking hydrogen bonds can generally be used as the debonding agent of the present invention. In particular, as described above, it is generally desirable that the debonding agent has a positive valence to form an ionic bond with an anionic group on the cellulose fiber. Some suitable positive debonding agents include, but are not limited to, quaternary ammonium compounds, imidazolinium compounds, bis-imidazolinium compounds, diquaternary ammonium compounds, polyquaternary ammonium compounds, ester functional quaternary ammonium compounds (ie, tetrafatty acid trialkanes) Ester salts), phospholipid derivatives, polydimethylsiloxane and related cationic and nonionic silicone resin compounds, fat and carboxylic acid derivatives, monomers and glycan derivatives, polyoxygen Pages (please note and use continuation pages when the invention description page is insufficient) PKOOl-0818-Becky-20030220 -February 20, 2003 \ η 200300810 Invention description $ Sell and buy; Shiyan hydrogen compounds and so on. For example, some suitable debonding agents are described in

Jenny等人的美國專利第5丨了6498號;Wendt等人的5730839 號,Keys等人的621 1 139號;Phan等人的5543067號;以 及歐洲專利WO/0021918,爲了參考,其内容於此併入之。 舉例來説,Jenny等人和Phan等人描述了許多種適用於本發 月的S日類έ把基的季鍵去鍵結劑(即四級脂肪酸三燒烴胺酯 鹽)。此外,Wendt等人描述了適用於本發明的imidaz〇linium 四級去键結劑。進一步地,Keys等人描述了可用於本發明的 聚酯聚季銨去鍵結劑。 其他合適的去鍵結劑描述於Kaun的美國專利第 5^9665號以及Funk等人的5558873號,爲了參考,這些内 谷於此併入之。尤其,Kaun揭示了使用各種陽離子矽樹脂組 成物作爲柔軟劑。 雖然反應組成物,如上所述,可加到纖維素纖維中來幫 助乳膠留置其上,但亦應瞭解到此類組成物亦可在乳膠添加 後使用。尤其,本發明並限制乳膠和反應組成物的添加順 序。例如’在一實施例中,乳膠,濕強度劑和去鍵結劑可連 %地加到織物中。在另一實施例中,濕強度劑,乳膠和去键 結劑可連續地加到織物中。 根據本發明所製的薄紙製品通常可根據此項技術已知 的各種造紙方法來製造。事實上,任何能夠製造紙類織物的 程序皆可用在本發明中。例如,本發明的造紙程序可利用濕 壓’起續,經空氣乾燥,起縐經空氣乾燥,不起縐經空氣乾 燥,一次重複起縐,二次重複起縐,砑光,印花,空氣鋪設, 18 200300810 發明說明 以及其他處理紙類織物的步驟。 ~~^一~ - 在某些實施例中,除了使用各種化學處理外,如上所 述,造紙程序本身亦可選擇性地改變來產生具有料性質的 薄紙製品。例如,可利用造紙程序來形成-多層紙類織物, 如Farrington,Jr•等人所揭示的美國專利第5129988號; Edwards寺人的5494554號;以及κ麵的5529665號,其内 容於此併入參考之。 疒這方面,各種形成多層紙類織物的方法實施例現在 將被描述得更加詳細。請參考第—圖,其顯示—種根據本發 明之-實施例的製造一濕壓薄紙的方法,同時參考鋪置成 形,其中兩濕織物層個别被形成,然後結合在一起形成一單 -織物。爲了形成第-織物層’以造紙技術中已知的方式來 至被-纖維(不論硬木或軟木),然後將此纖維輸送到第一原 料槽⑴’其中纖維以懸浮溶液的形式被儲存…原料幫浦⑺ 將所需要的懸浮液量供應至風扇幫浦⑷的抽吸侧。若期望的 ,’―計量幫浦(5)可供應—添加劑(即乳膠,反應組成物等 幸)至纖㈣m料㈣釋水(3)亦與纖輔浮液混合。 目然後,全部的纖維混合物被加壓並輸送至前頭E (6)。水 懸浮液離開前頭E⑹且沈置在抽吸箱⑻上方的環狀造紙組 織⑺上。抽吸箱内的壓力是眞空以下而可吸出懸浮液中的 水,因此形成第一層。在這個範例中,從前頭匣⑹流出的原 料會被當作“空4御Γ I ’最後乾燥期間,此層會被放在遠 離乾燥表面的位置。 成形組織可爲任何成形織品,例如纖維支持指數15〇或 19 200300810U.S. Patent No. 5,998, Jenny et al .; 5,730,839 Wendt et al .; 621 1 139, Keys et al .; 5,430,67, Phan et al .; and European Patent WO / 0021918, the contents of which are hereby incorporated by reference. Incorporate it. For example, Jenny et al. And Phan et al. Describe a variety of quaternary bond debonding agents (ie, quaternary fatty acid trisalinated hydrocarbon amine esters) that are suitable for the S-class bases of this month. In addition, Wendt et al. Describe imidazolin quaternary debonding agents suitable for use in the present invention. Further, Keys et al. Described polyester polyester quaternary debonding agents useful in the present invention. Other suitable debonding agents are described in Kaun U.S. Patent No. 5,9665 and Funk et al. 5,558,873, which are incorporated herein by reference. In particular, Kaun discloses the use of various cationic silicone resin compositions as softeners. Although the reaction composition, as described above, can be added to cellulose fibers to help the latex stay on it, it should also be understood that such a composition can also be used after the latex is added. In particular, the present invention does not limit the order of addition of latex and reaction composition. For example, in one embodiment, latex, wet strength agent, and debonding agent may be added to the fabric in percent. In another embodiment, wet strength agents, latex and debonding agents may be added to the fabric continuously. Tissue paper products made according to the present invention can generally be made according to various papermaking methods known in the art. In fact, any procedure capable of making paper fabrics can be used in the present invention. For example, the papermaking process of the present invention can use wet pressing to start, air dry, crepe air dry, not crepe air dry, repeat crepe once, repeat crepe, calender, print, air laying , 18 200300810 Description of the invention and other steps for processing paper fabrics. ~~ ^ 一 ~-In some embodiments, in addition to using various chemical treatments, as described above, the papermaking process itself can be selectively modified to produce tissue paper products with material properties. For example, a papermaking process can be utilized to form a multi-layer paper fabric, such as US Patent No. 5,129,988 disclosed by Farrington, Jr., et al .; Edwards Temple No. 5,494,554; and kappa surface No. 5,526,665, the contents of which are incorporated herein Refer to it. In this regard, various embodiments of the method for forming a multilayer paper fabric will now be described in more detail. Please refer to the figure, which shows a method for manufacturing a wet-pressed tissue paper according to an embodiment of the present invention, while referring to laying forming, in which two wet fabric layers are individually formed and then combined to form a single- Fabric. In order to form the -fabric layer 'come the duvet-fibers (whether hardwood or softwood) in a manner known in papermaking technology, and then transport this fiber to the first raw material trough' where the fibers are stored in the form of a suspension solution ... Pump pump supplies the required amount of suspension to the suction side of the fan pump pump. If desired, the metering pump (5) can be supplied with additives (ie, latex, reaction composition, etc.) to the fiber release water (3) is also mixed with the fiber-assisted floating liquid. The entire fiber mixture is then pressurized and delivered to the front E (6). The water suspension leaves the front E⑹ and sinks on the endless papermaking tissue ⑺ above the suction box ⑻. The pressure in the suction box is below the emptiness and the water in the suspension can be sucked out, so the first layer is formed. In this example, the raw material flowing out of the head box ⑹ will be regarded as the "empty 4 Yu Γ I 'during the final drying, this layer will be placed away from the dry surface. The forming structure can be any forming fabric, such as fiber support Index 15 or 19 200300810

發明說明liM 更大的組織。某些合適的成形組織包括(但不限制於此)單層 組織,如得自 Albany International Corporation,Appleton Wire Division,Menasha,Wis·的 Appleton Wire 94M ;雙層組 織,如得自 Asten Group,Appleton,Wis·的 Asten866 ;以及 三層組織,如得自 Lindsay Wire,Florence,Miss 的 Lindsay3080 ° 造紙纖維離開前頭匣時的懸浮水溶液濃度爲〇 〇5%至 2%之間,且在一實施例中爲〇·2%。第一前頭匣(6)可爲具有 二或更多分層隔間的分層前頭匣,而可輸送分層的第一濕織 物層,或者可爲輸送混合或同質之第一濕織物層的單層前頭 匡。 爲了形成第二織物層,以造紙技術中已知的方式來製備 特定的纖維(無論硬木或軟木)且將此纖維送到第二原料槽 (11),其中纖維是以懸浮水溶液的形式儲存於其中。一原料 幫浦(丨2)將所需要的懸浮液量供應至風扇幫浦(14)的抽吸 侧。一計量幫浦(5)可供應添加劑(即乳膠,反應組成物等等) 至如上所述的纖維懸浮液中。額外的稀釋水(13)亦與纖維懸 浮液混合。然後,全部的纖維混合物被加壓並輸送至前頭匣 (16)。水懸浮液離開前頭厘(16)且沈置在抽吸箱(18)上方的環 狀造紙組織(17)上。抽吸箱内的壓力是眞空以下而可吸出懸 浮液中的水,因此形成第二濕織物。在這個範例中,從前頭 11(16)流出的原料會被當作“較乾燥側”,這是因爲此層最 後會與乾燥表面接觸。適合形成第二前㈣之組織(17)的成 开八组、、哉包括先則提及用來形成第一前頭匣成形組織的成形 續頁) a續次頁 ΡΚ001-0818-Bee 20 200300810 發明說明$賣胃 材料。 一4 土卜和第二濕織物層出成形之後,此二織物層被帶在 :起而互相接觸(以平鋪的形式),而濃度爲ι〇%至3〇%之 :1二::濃度爲荷,通常期望兩濕織物的濃度大體上相同。 2㈣-濕織物層與滾輪(19)上的第二濕織 到平鋪方式接觸的目的。 曰此接觸在-起的織物被送到眞空箱(20)上的毛氈上 争可以傳統方法來讓此結合在一起的織物脱水,乾燥和起 更具體來説,此平鋪的被進—步地脱水並輸送到一使用 …輪(31)的乾燥機(3〇)(即楊基乾燥機)上,其用來將織物中 勺K刀擠出(足些水會被毛氈吸收)且讓織物黏在乾燥機的表 面上。然後’織物被乾燥,選擇性地起㈣捲緩在滾輪(32) 上’以隨後能轉變成最終起縐產品。 第二圖爲可用在本發明造紙程序之另一實施例的流程 圖舉例來説,其顯示了一分層前頭Ε (41),_成形組織 (42),一成形滾輪(43),一造紙毛氈(44),一壓輪(45),一楊 基乾燥機(46)和一起縐刮刀(47)。此外另顯示了(未標號)多種 齒輪或用來界定圖示中之組織的拉緊滾輪,其實際作用時可 以不同。在操作上,分層前頭匣連續地將一分層原料射在成 形組織(42)和毛氈(44)之間,此分層原料射出物部份地纏裹 在成形滾輪(43)上。當新成形的織物橫越成形滾輪的弧形部 份時,通過成形組織(42)之懸浮水溶液的水分藉著離心力而 被除去。當成形織物(42)和毛氈(44)分開,濕織物會與毛氈(44) 在一起且被送到楊基乾燥機(46)上。 pii續次頁(發明說明頁不敷使用時,請註記並使用續頁) 2 1 ^〇〇l-〇818-Becky-20030220 -February 20, 2003 2UUJU0810 發明說明It;;Invention description liM larger organization. Some suitable shaped tissues include, but are not limited to, single-layer tissues, such as those available from Albany International Corporation, Appleton Wire Division, Menasha, Appleton Wire 94M, Wis; double-layer tissues, such as obtained from Asten Group, Appleton, Wis · Asten866; and a three-layer structure, such as Lindsay 3080 ° from Lindsay Wire, Florence, Miss, when the papermaking fiber leaves the front box, the concentration of the suspended aqueous solution is between 0.05% and 2%, and in one embodiment is 0.2%. The first front box (6) may be a layered front box having two or more layered compartments, and may convey a layered first wet fabric layer, or may be a mixed or homogeneous first wet fabric layer. Single layer front. In order to form the second fabric layer, specific fibers (whether hardwood or softwood) are prepared in a manner known in papermaking technology and sent to a second raw material tank (11), where the fibers are stored in the form of a suspended aqueous solution in among them. A raw material pump (2) supplies the required amount of suspension to the suction side of the fan pump (14). A metering pump (5) can supply additives (ie, latex, reaction composition, etc.) to the fiber suspension as described above. Additional dilution water (13) is also mixed with the fiber suspension. The entire fiber mixture is then pressurized and delivered to the headbox (16). The aqueous suspension leaves the front centimeter (16) and is settled on a ring-shaped papermaking structure (17) above the suction box (18). The pressure in the suction box is below the emptiness and the water in the suspension can be sucked out, thus forming a second wet fabric. In this example, the material flowing out of the front 11 (16) is considered as the “dryer side” because this layer will eventually come into contact with the dry surface. Eight groups of openings (17) suitable for forming the second frontal structure (17), including the first mentioned the forming continuation sheet used to form the first front box forming structure) a continuation page ΡΚ001-0818-Bee 20 200300810 Invention Description $ sells stomach material. 1-4 After the soil cloth and the second wet fabric layer are formed, the two fabric layers are brought into contact with each other (in the form of a tile), and the concentration is ι0% to 30%: 1: 2: The concentration is charged, and it is generally expected that the concentration of the two wet fabrics is substantially the same. 2㈣-The purpose of the wet fabric layer in contact with the second wet-to-tile pattern on the roller (19). The contacted fabric is sent to the felt on the empty box (20). The traditional method can be used to dehydrate, dry and lift the combined fabric. More specifically, the tile is further advanced. It is dewatered and conveyed to a dryer (30) (that is, a Yankee dryer) using a ... wheel (31), which is used to squeeze the k-knife out of the fabric (the water will be absorbed by the felt) and let The fabric sticks to the surface of the dryer. The 'fabric is then dried and selectively rolled onto a roller (32)' to be subsequently transformed into the final creped product. The second figure is a flowchart which can be used in another embodiment of the papermaking process of the present invention. For example, it shows a layered front E (41), a forming structure (42), a forming roller (43), and a papermaking. Felt (44), a pressure roller (45), a Yankee dryer (46) and a crepe scraper (47). In addition, a variety of gears (not labeled) or tensioning rollers used to define the organization shown in the figure are shown, and their actual effects can be different. In operation, the layered front head box continuously shoots a layered raw material between the forming tissue (42) and the felt (44), and the layered raw material ejection is partially wrapped around the forming roller (43). As the newly formed fabric traverses the arc-shaped portion of the forming roller, the water in the suspended aqueous solution passing through the forming tissue (42) is removed by centrifugal force. When the forming fabric (42) is separated from the felt (44), the wet fabric will be with the felt (44) and sent to the Yankee dryer (46). pii continuation page (please note and use the continuation page when the invention description page is insufficient) 2 1 ^ 〇〇l-〇818-Becky-20030220 -February 20, 2003 2UUJU0810 Invention Description It;

在揚基乾燥機(46)卜膝 ----一I 浮液形式的黏著劑頂部。此,容二用的化學劑被連續加到懸 加,如使用噴灑器,1可平均U利用任何方便的方式來添 機表面上。乾燥機(46;“ 續黏著溶液喷灑在乾燥 處理到刀(ο)之I 上的添加點會立即接在起鱗起縐 和乾燥。 讀鮮的黏著劑薄膜有足夠時間能散佈 到織::些::',乳膠’反應組成物等在乾燥時可被添加 Π今血士始* 的使用。舉例來説,喷滋器可以分 I :著劑—起將添加劑加到鼓㈣上,使織物通過 乂二:、Γ劑被加到織物的外層上。在某些實施例中, 乾餘機(46)表面上的添加點立即接著 新鮮的黏著劑薄膜在盥厭认+^ ^ …“: 中的織物接觸前能有足夠時 ^ _°將添加劑加到乾燥鼓的方法和技術在Smith :人的美國專利第5853539號和Smith等人的59936G2號中 有更詳細的描述,爲了參考,這些内容於此併入之。 濕織物藉一具有施加壓力的壓輪⑹來鋪在乾燥機(46) 表面上’在-實施例中,此施加壓力爲每平方英叶2〇〇磅 ㈣。在壓緊或脱水步驟之後,織物的濃度通常爲3〇%或以 上。足夠的楊基乾燥機蒸汽能量和罩蓋乾燥能力被施加到此 織物上,使最終濃度達95%或以上,具體來説是97%或以上。 薄片或織物溫度會立即超過起縐刮刀(47),例如,依紅外線 溫度感應器測量所得,其溫度通常爲250卞。 織物亦可使用非壓縮乾燥技術來乾燥,如經空氣乾燥。 經空氣乾燥機是藉著使空氣通過織物卻不施加任何機械壓 22 200300810 發明說明®頁 力來達到將水分從織物除去的效果。經空氣乾燥可增加織物 的體積和柔軟度。此類技術的範例揭示於CGQk等人的美國 專利第5048589號;Sudall等人的5399412號;等 人的5510001號;Rug〇wski等人的55913〇9號;以及 等人的601 74 17號,這些内容於此併入參考之。 例如,參考第三圖,其圖示了造紙機器之一實施例,此 造紙機器可用來成形一不起縐的經乾燥薄紙製品。爲了簡潔 易懂,各種用來大致界定數組織移動的拉緊滾輪被顯示出來 而沒有標號。如圖所示,一造紙前頭匣(11〇)可用來將造紙纖 維g浮水溶液射出或放置在一上成形組織(丨丨2)上。然後,纖 維的懸浮水溶液被送到一較低的成形組織(11 3)上,其可用來 支撐並攜帶此新成形的濕織物(111)在程序中向下移動。若期 望的話,在濕織物(111)被成形組織(113)支撐的期間可以完 成濕織物(111)的脱水,如藉著眞空抽吸來達成。 然後,濕織物(111)從成形組織(113)被送到輸送組織 (U7),期間濕織物(111)的固體濃度爲10%至35%,具體來 説介於20%至30%之間。於此使用之“輸送組織”是一種位 在織物製造程序中之成形區和乾燥區之間的組織。在此實施 例中’輸送組織(11 7)爲一具有突出物或壓印痕的有圖案組 織’如Wendt等人於美國專利第6017417號中所描述者。通 常’輸送組織(117)的移動速度低於成形組織(113)的速度, 以提高織物的“ MD伸張性”,其通常是指織物在其機器戈 長度方向上的伸張力(以失敗樣本的拉身百分比表示)。例 如,兩組織之間的相對速度差異可介於〇%至80%之間,在 E]續次頁(發明說明頁不敷使用時,請註記並使用續頁) PK〇〇I-〇8I8~Becky-20030220 -February 20, 2003 23 200300810 發明說明,f賣Μ 某些實施例中大於1G%,而在某些實施例中介# ι〇%至 60%’且在某些實施例中介於15%至3〇%。這個一般是指“快 速輸送。執行快速輸送的其中一種有用方法説明於Engel 等人的美國專利第5667636號,其内容爲了參考於此併入之。 輸送到組織(117)可藉著正及/或負壓來達成。例如,在 一實施例中,眞空鞋(118)可提供負壓,使成形組織(113)和 輸送組織(11 7)同時於眞空狹縫的帶領邊緣會合並分歧。通 常,眞空鞋(118)所供應的壓力介於1〇至25英吋水銀高度。 如上所述,眞空輸送鞋(丨i 8)(負壓)可藉使用織物相對側的正 壓來補充或取代,以將織物吹到下一個組織。在某些實施例 t,其他眞空鞋亦可用來幫助將纖維組織(111)吸引到輸送組 織(117)的表面上。 然後,從輸送組織(117),纖維組織(m)被送到經乾燥 組織(11 9)上。當濕織物(1丨丨)被經乾燥組織(113)所支撐時, 織物(1 1 1)會被經乾燥機(121)乾燥使其固體濃度爲95%或更 大。此經乾燥機(121)藉著讓空氣通過織物(m)而沒有施加 任何機械壓力來將水分從織物(丨n)中移除。經乾燥亦可增加 織物(111)的體積和柔軟度。例如,在一實施例中,經乾燥機 (121)可包含一可旋轉的,穿孔的圓筒以及一罩蓋,罩蓋可在 經乾燥組織(119)攜帶織物(111)通過圓筒上部時,接收圓筒 穿孔吹出的熱空氣。加熱的空氣被強迫通過經乾燥機(丨2 i) 的圓同牙it並將織物(111)中的剩餘水分去除。被經乾燥機 (121)強迫通過織物(111)的空氣溫度是可以改變的,但通常 介於250F至500p之間。亦應瞭解到,其他不壓縮的乾燥 [3續次頁(發明說明頁不敷使用時,請註記並使用續頁) PK001-0818-Becky-20030220 -February 20, 2003 24 200300810 發明說明$賣頁 方法’如微波或紅外線加熱也可使用。 如上所述,當織物依程序通過造紙機器時,乳膠有時可 加到織物上。例如’在—特定實施例中,乳膠可以喷麗到織 物上。噴灑作用可以提高乳膠大體維持在織物外層上的能 力,藉以更佳地约束織物外層上的脱落。大致上,乳膠可在 織物成形期間的任何時候喷灑到它上面。例如,在如第三圖 所式的-實施例申,一喷嘴(140)可在織物(111)被送到織物 足後以及它被乾燥之前,將乳膠喷到織物(in)上。然 而,應瞭解到,喷嘴(14〇)可位在任何期望的位置上。 任何適用來將添加劑喷灑到一紙類組織上的設備皆可 用於本發明。例如’其中一合適的喷灑設備例子包括外部混 合,空氣霧化噴嘴,如得自V.j.B Systems,Inc (位在Tucker, Ga·)的2mm喷嘴。另一種可使用的喷嘴爲得自On the Yankee Dryer (46), the knee is a top of the adhesive in the form of a floating liquid. Therefore, the chemical used in Rongji is continuously added to the suspension. If a sprayer is used, 1 can be added to the surface of the machine in any convenient way. The dryer (46; "continuous adhesive solution sprayed on the drying point to the knife (ο) I will be immediately connected to the scale and crepe and dry. Read the adhesive film has enough time to spread to the weaving: : Some :: ', latex' reaction composition can be added when the blood is dry *. For example, the spray nozzle can be divided into I: the agent-add the additive to the drum, The fabric is passed through the two layers: The agent is added to the outer layer of the fabric. In some embodiments, the point of addition on the surface of the dryer (46) is immediately followed by a fresh adhesive film in the bathroom + ^ ^… ": The fabric can be used for a sufficient time before contact. The method and technique for adding additives to the drying drum are described in more detail in Smith: U.S. Patent No. 5,853,539 and Smith et al., 59936G2, for reference. These are incorporated herein. The wet fabric is spread on the surface of the dryer (46) by a pressure roller ⑹ with an applied pressure. In the embodiment, the applied pressure is 200 pounds per square inch After the compaction or dehydration step, the concentration of the fabric is usually 30% or more. The Yankee dryer's steam energy and hood drying capacity are applied to this fabric to achieve a final concentration of 95% or more, specifically 97% or more. The temperature of the sheet or fabric will immediately exceed the crepe scraper (47) For example, the temperature measured by an infrared temperature sensor is usually 250 ° C. The fabric can also be dried using non-compressive drying technology, such as air drying. The air dryer is used to pass air through the fabric without applying any machinery. Press 22 200300810 Description of the invention® sheet force to achieve the effect of removing moisture from the fabric. Air drying increases the volume and softness of the fabric. Examples of such techniques are disclosed in US Patent No. 5048589 by CGQk et al .; Sudall et al. No. 5399412; et al. 5510001; Rugowski et al. 55913〇9; and et al. 601 74 17 are incorporated herein by reference. For example, refer to the third figure, which illustrates An embodiment of a papermaking machine that can be used to form an uncreped dried tissue product. For simplicity and ease of understanding, various tensions are used to roughly define the movement of the tissue. The wheels are shown without labels. As shown in the figure, a papermaking head box (11) can be used to eject or place a floating solution of papermaking fiber g on an upper forming structure (丨 丨 2). Then, a suspension aqueous solution of the fibers Is sent to a lower formed tissue (11 3) which can be used to support and carry this newly formed wet fabric (111) down during the procedure. If desired, the wet fabric (111) is formed tissue (113) The dehydration of the wet fabric (111) can be completed during the support period, such as by emptying. Then, the wet fabric (111) is sent from the forming tissue (113) to the conveying tissue (U7), during which the wet fabric The solid concentration of (111) is 10% to 35%, specifically between 20% and 30%. As used herein, a "conveying structure" is a structure that is located between a forming area and a drying area in a fabric manufacturing process. In this embodiment, the 'transporting tissue (117) is a patterned tissue with protrusions or embossing marks' as described in Wendt et al., U.S. Patent No. 6017417. Generally, the moving speed of the conveying tissue (117) is lower than that of the forming tissue (113) to improve the "MD stretchability" of the fabric, which usually refers to the tensile tension of the fabric in the direction of the length of the machine (in terms of failed samples) Pull percentage indicated). For example, the relative speed difference between the two organizations can be between 0% and 80%. E] continued page (if the invention description page is insufficient, please note and use the continued page) PK〇〇I-〇8I8 ~ Becky-20030220 -February 20, 2003 23 200300810 Description of the invention, in some embodiments, it is greater than 1G%, and in some embodiments, it is between #% and 60%, and in some embodiments it is between 15% and 15%. % To 30%. This generally refers to "rapid delivery. One useful method of performing rapid delivery is described in US Patent No. 5,667,636 to Engel et al., The contents of which are incorporated herein by reference. Delivery to tissue (117) can be achieved by / For example, in one embodiment, the empty shoes (118) can provide negative pressure, so that the forming tissue (113) and the conveying tissue (117) will merge at the leading edge of the empty slit at the same time. The pressure supplied by the empty shoes (118) is between 10 and 25 inches of mercury. As mentioned above, the empty shoes (丨 i 8) (negative pressure) can be supplemented or replaced by using positive pressure on the opposite side of the fabric. To blow the fabric to the next tissue. In some embodiments, other empty shoes can also be used to help attract fibrous tissue (111) to the surface of the transport tissue (117). Then, from the transport tissue (117), The fibrous tissue (m) is sent to the dried tissue (11 9). When the wet fabric (1 丨 丨) is supported by the dried tissue (113), the fabric (1 1 1) is passed through the dryer (121) Dry to give a solid concentration of 95% or more. This is dried (121) Remove moisture from the fabric (n) by passing air through the fabric (m) without applying any mechanical pressure. Drying can also increase the volume and softness of the fabric (111). For example, in a In an embodiment, the dryer (121) may include a rotatable, perforated cylinder and a cover, and the cover may receive the cylinder when the dried tissue (119) carries the fabric (111) through the upper part of the cylinder. The hot air blown out by the perforation. The heated air is forced to pass through the circular teeth of the dryer (丨 2 i) and removes the remaining moisture in the fabric (111). It is forced through the dryer (121) through the fabric (111) The temperature of the air can be changed, but it is usually between 250F and 500p. It should also be understood that other uncompressed drying [3 Continued page (if the invention description page is insufficient, please note and use the continued page) PK001 -0818-Becky-20030220 -February 20, 2003 24 200300810 Description of the invention $ Sale method 'such as microwave or infrared heating can also be used. As mentioned above, latex can sometimes be added to the fabric when the fabric passes through the paper machine according to the procedure. ... such as 'in-specific embodiments' Latex can be sprayed onto the fabric. Spraying can improve the ability of the latex to generally maintain on the outer layer of the fabric, thereby better restraining the shedding on the outer layer of the fabric. In general, latex can be sprayed onto the fabric at any time during the fabric formation Above, for example, in the embodiment shown in the third figure, a nozzle (140) can spray the latex onto the fabric (in) after the fabric (111) is fed to the fabric foot and before it is dried. However, it should be understood that the nozzle (14) can be positioned at any desired position. Any device suitable for spraying additives onto a paper tissue can be used in the present invention. For example, 'one example of a suitable spraying device includes an external mixing, air atomizing nozzle, such as a 2 mm nozzle available from V.j.B Systems, Inc (Tucker, Ga.). Another usable nozzle is available from

Systems,Inc.(位在 Milwaukee,Wisc〇nsin)的 η 1/8” vV-SS 650017 VeeJet噴嘴。其他喷灑技術和設備描述於Ampuls]d 等人的美國專利第5164(M6號,其内容於此併入參考之。 根據本發明,有十會期望控制乳膠留在纖維素纖維上的 田存百分率。明確來説,一或更多變數,如乳膠及反應組成 物的添加順序,乳膠種類,反應組成物的種類,乳膠和反應 組成物的添加量等等,皆可選擇性地改變以使最終留存百分 率在理想的範圍内。舉例來説,在某些實施例中,會期望乳 膠留在纖維上的百分比至少6〇%,而在某些實施例中,則介 於75%至90%之間。 乳膠留在纖維素纖維上的留存百分率可根據下列公式 Q續次頁 PK001 - 0818-Bee _麵醜顧) 25 200300810 發明說明,_:!; 來決定: 留存百分率(%) = 1〇〇x[(Lt — Lf)/Lt] 其中Systems, Inc. (Milwaukee, Wisconsin) η 1/8 "vV-SS 650017 VeeJet Nozzle. Other spraying techniques and equipment are described in U.S. Pat. No. 5164 (M6, the contents of which According to the present invention, there are ten desires to control the percentage of latex remaining on cellulose fibers. Specifically, one or more variables, such as the order of adding latex and reaction composition, the type of latex The type of the reaction composition, the addition amount of the latex and the reaction composition, and the like can be selectively changed so that the final retention percentage is within a desired range. For example, in some embodiments, it is expected that the latex retention The percentage on the fiber is at least 60%, and in some embodiments it is between 75% and 90%. The retention percentage of the latex on the cellulose fiber can be based on the following formula Q Continued PK001-0818 -Bee _ 面 鬼 顾) 25 200300810 Description of the invention, _:!; To decide: Percent retention (%) = 100 × [(Lt — Lf) / Lt] where

Lt爲乳膠加到紙漿中的總量;而Lt is the total amount of latex added to the pulp; and

LF爲將紙漿從過濾物移除後,乳膠留在過濾物中的量。 舉例來説,LF可以藉著過濾物的“混濁”値來決定。於此使 用之“混濁” 一詞通常是指一物質的光學清晰度,其可被測 量,例如使用得自 HF Scientific,lnc.的 Model DRT 100B 混 濁,則1儀來測量,其測出的混濁度以“懸液混濁單位”(N叫 來表示。舉例來説,在一實施例中,可使用已知的“^”値 來建立一線性回歸方程式,即LF=ax+b,並 广 爲定値,而“X”爲混濁値。 ”中a和b 藉著控制乳膠的留存百分率,加到薄紙製品的強度和§ 硬度可依期望適當地平衡。再者,較高的留存百分率能允言LF is the amount of latex remaining in the filter after the pulp is removed from the filter. For example, LF can be determined by the "turbidity" of the filter. The term "turbidity" as used herein generally refers to the optical clarity of a substance, which can be measured, for example, using a Model DRT 100B turbidity from HF Scientific, lnc. The degree is expressed as "suspension turbidity unit" (N. For example, in an embodiment, a known "^" 値 can be used to establish a linear regression equation, that is, LF = ax + b, and is widely used The "X" is turbidity. "A" and "B" in the "by controlling the retention percentage of latex, the strength and rigidity added to tissue paper products can be properly balanced as desired. Furthermore, a higher retention percentage can allow

-較低的總乳膠量,如果留存百分率較低的話。所以,因肩 需要一較低的乳膠量,本 I J ^ k供讓花費有相當程度白彳 降低’並提高造紙程序的效率真去 . 双手再者,瑕終薄紙製品可較弱 健且產生較低置的棉織和脱% 同陆 贶6,冋時痕瑕終的薄紙製品維和 理想的彈性和柔軟度。 範例 由混濁値決定乳膠維持能力係被證明。首先,由1( 白牛皮紙軟木《纖維來製備—纖維泥製。此 顚粉碎機中粉碎5分鐘,使並固髀、、f a U 辰度爲1·6%。然後,-Lower total latex, if the retention percentage is lower. Therefore, because the shoulder needs a lower amount of latex, the IJ ^ k supply cost can be reduced to a certain extent, and the efficiency of the papermaking process is really improved. With both hands, flawed tissue paper products can be weaker and produce more Low-position cotton weaving and stripping% Same as Luan 6, the thin paper products at the end of the flaws maintain ideal elasticity and softness. Example Latex maintenance capacity determined by turbidity is proven. First, it is made from 1 (white kraft paper cork fiber—made from fiber mud. This pulverizer is pulverized for 5 minutes, so that the f, U, and f a U can be 1.6%. Then,

S續次頁 PK00J-08J8-B (發明說明頁不敷使用時 ecky-20030220 -February 20. 2003 請註記並使用 續頁) 26 200300810 發明說明$賣頁 浆稀釋至濃度爲0.33%。 然後’從紙漿中取出四份纖維原料樣本(體積909 nd, 重里_ 3 a克),並把它們分别放在一燒杯内。之後,將一陰離 子苯乙歸-丁二烯乳膠溶液(固體含量(依溶液重量)爲 得自D〇w Chemica卜商標“ dl_239”),加到各纖維 原料樣本中,其添加量分别如表一所示。 旦加入乳膠,用水將原料樣本稀釋成1 〇〇〇㈤丨。然後 等10分鐘,根據TAPPPI測試方法τ227讓樣本通過自由測 試器(Freeness Tester)的網篩來過濾。S Continued page PK00J-08J8-B (When the description page of the invention is insufficient, ecky-20030220 -February 20. 2003 Please note and use continued page) 26 200300810 Description of the invention $ Sale page The slurry is diluted to a concentration of 0.33%. Then ‘take four samples of fiber material (volume 909 nd, weight_ 3 ag) from the pulp and place them in a beaker. Then, an anionic acetophenone-butadiene latex solution (solid content (depending on the weight of the solution) was obtained from Dow Chemica brand "dl_239") was added to each fiber raw material sample, and the addition amounts were as shown in the table As shown. Once the latex is added, the raw material sample is diluted to 1000 Å with water. Then wait for 10 minutes and pass the sample through a Freeness Tester screen to filter according to the TAPPPI test method τ227.

收集底邵和側孔的過濾物,並把它們混合在一起以供 此’蜀度測量。陰離子乳膠在纖維素材料織物上的存量會 萃曰著測里材料的“混濁度”來測定。明確來説,Model DRT 100B /m濁測量儀得自hf Scientific,Inc.,其先用一試管中 的標準溶液來校正。然後收集4〇毫升的過濾物並加到試管 中。然後將此事管放在混濁測量儀中,此測量儀具有一光 源’而可提供與試管垂直的光線。然後從混濁測量儀上讀出 最終混濁値並記綠之。 各樣本的最終結果皆與一不含紙漿的控制樣本比較。其 結果亦顯示於表一。 表一:混濁値測試結果 樣本 乳膠量 (lbs/ton) 混濁値 含紙漿 不含紙漿 控制組 0 44.4 N/A 1 5 52 47 2 10 87 83 Ξ續次頁 ΡΚ00 ]-08 I8-Bec (發明說明頁不敷使用時,請註記並使用續頁) ky- 2 0 〇 3 0 2 2 0 -February 20, 2003 27 200300810 發明說明1賣頁 3 20 165 1 60 4 40 1 274 X \J \J __268 --—-—— 如上所示’在相同添加量的乳膠下,轉樣本的過減物 比控制樣本㈣物的混濁値稍高。雖然不被理論限制,應相 信此結果所得出的事實’就是小量的紙漿顆粒就會影響混濁 値。 當纖維被篩選之後,留存在過濾物中的乳膠量會藉由建 王-回歸方程式來測量,其中乳膠在過渡物中的殘量⑽/每 :我桌)爲y變數,而測量所得的控制樣本混濁値爲“ χ” 走數在表所&供的數據中,最終回歸方程式爲: y = 0.l504x— 1.8589,其中相關係數(R2)等於 〇 99。 範例二 乳將與纖維原料的結合能力被證明。首先,由10%漂白 T皮紙軟木紙漿纖維來製備一纖維泥漿。此泥漿在一不^顚 粉碎機中粉碎5分鐘,使其固體濃度爲16%。然後,將泥漿 稀釋至濃度爲0.33%。 然後,從紙漿中取出六份纖維原料樣本(體積9〇9 ml, 重量3公克),並把它們分别放在丨〇〇〇 mi燒杯内。之後,將 陰離子表乙埽_丁二埽乳膠溶液(固體含量(依溶液重量)爲 〇-5°/〇)(得自Dow Chemical,商標“DL-239”)加到各纖維原 料心本中’添加量分别爲2〇比/丁。此外,一咪峻口林四級去鍵 結劑(得自 Hercules,inc·,商標名稱爲“ Pr〇s〇ft TQ-1〇〇3”) 和“Parez”聚丙烯醯胺暫時濕強度劑(亦作爲乾強度劑)也 户思/續發1 說曰月?不敷使用時,請註記並使臓頁)The bottom and side filters were collected and mixed together for this measurement. The amount of anionic latex on the cellulosic fabric will be determined by measuring the "turbidity" of the material. Specifically, the Model DRT 100B / m turbidimeter was obtained from hf Scientific, Inc., which was first calibrated with a standard solution in a test tube. 40 ml of the filtrate was then collected and added to a test tube. This tube is then placed in a turbidity measuring instrument, which has a light source ' and provides light perpendicular to the test tube. Then read the final turbidity from the turbidity meter and record it green. The final results of each sample were compared with a control sample without pulp. The results are also shown in Table 1. Table 1: Turbidity test results Sample emulsion amount (lbs / ton) Turbidity test with pulp without pulp Control group 0 44.4 N / A 1 5 52 47 2 10 87 83 Ξ Continued on page PK00] -08 I8-Bec (Invention When the description page is insufficient, please note and use the continuation page) ky- 2 0 〇3 0 2 2 0 -February 20, 2003 27 200300810 Invention Description 1 Selling page 3 20 165 1 60 4 40 1 274 X \ J \ J __268 ----------- As shown above 'At the same amount of latex, the excess of the sample transferred is slightly higher than the turbidity of the sample. Although not limited by theory, it is believed that the result of this result 'is that a small amount of pulp particles will affect the turbidity. After the fiber is screened, the amount of latex remaining in the filter will be measured by the King-Regression equation, where the residual amount of the latex in the transition (⑽ / per: US) is the y variable, and the measured control The sample turbidity is “χ”. In the data provided in the table, the final regression equation is: y = 0.l504x—1.8589, where the correlation coefficient (R2) is equal to 099. Example 2 The ability of milk to combine with fiber raw materials is demonstrated. First, a fiber slurry was prepared from 10% bleached T-paper cork pulp fibers. This slurry was pulverized for 5 minutes in a pulverizer to make the solid concentration of 16%. Then, the mud was diluted to a concentration of 0.33%. Then, six samples of the fiber raw material (volume 109 ml, weight 3 g) were taken from the pulp, and they were placed in a 1000-m beaker. Thereafter, an anionic epithelium-butadiene latex solution (solid content (based on solution weight) of 0-5 ° / 〇) (available from Dow Chemical, trademark "DL-239") was added to each fiber material core 'The added amounts were 20 rations / d. In addition, Yimi Junkoulin Grade IV Debonding Agent (available from Hercules, inc., Under the trade name "PrOsft TQ-1〇03") and "Parez" Polyacrylamide temporary wet strength agent (Also as a dry strength agent) Yehusi / Renewal 1 Saying the month? (Insufficient use, please note and make the title page)

Becky-20030220 -February 20, 2003 28 200300810 發明說明$賣胃 被加到原料中,添加量分別爲16.5 lb/T和6.5 lb/T。這些添 加劑加到樣本中的添加順序,每樣本皆不同,其順序如表二 所示。每添加劑與下個添加劑的添加時間相隔5分鐘。 一旦加入添加劑,用水將原料樣本稀釋成1⑽〇 ml。25 分鐘後’根據範例一所述之方法讓樣本通過自由測試器 (Freeness Tester)的網篩來過濾。混濁度和乳膠留在過濾物中 的量依範例一所述者來決定。得到之後,根據下列公式,乳 膠留在過濾物中的量,被用來計算陰離子留在各種纖維素織 物上的留存百分率:Becky-20030220 -February 20, 2003 28 200300810 Description of the invention $ Selling stomach is added to the raw materials at 16.5 lb / T and 6.5 lb / T, respectively. The order in which these additives are added to the sample is different for each sample, and the order is shown in Table 2. Each additive is separated from the next additive by 5 minutes. Once the additives were added, the raw material samples were diluted to 100 ml with water. After 25 minutes', the sample was filtered through a Freeness Tester screen according to the method described in Example 1. The turbidity and the amount of latex remaining in the filter are determined as described in Example 1. After obtaining, according to the following formula, the amount of latex remaining in the filter is used to calculate the percentage of anion remaining on various cellulose fabrics:

留存百分率(%) = l〇〇x[(LT — LF)/LTJ 其中 LT爲乳膠加到紙漿中的總量;而 LF爲將紙漿從過濾物移除後,乳膠留在過遽物中的量。 結果如表二所示。 表二:樣本結果 樣本 第一添加 第二添加 第二添加 混濁値 留存率 1 去鍵結劑 乳膠 強度劑 38 —^_ 2 乳膠 去鍵結劑 強度劑 86 - Λ C 3 強度劑 去鍵結劑 乳U 51 J ~~__ 〇 r\ 4 &鍵結劑 強度劑 乳膠 卜37 5 乳膠 強度劑 去鍵結劑 66 ^^— 6 強度劑 乳膠 去鍵結劑 67 Λ0 ^_ 留存率。例 ’而有最小 如表所示,化學劑的添加順序可以影響乳膠 如,樣本1至4中,去键結劑是乳膠加之前家的 29 200300810Percent retention (%) = 100 × [(LT — LF) / LTJ where LT is the total amount of latex added to the pulp; and LF is the amount of latex remaining in the pulp after the pulp is removed from the filter. the amount. The results are shown in Table 2. Table 2: Sample results Sample first addition second addition second addition turbidity retention rate 1 debonding agent latex strength agent 38 — ^ _ 2 latex debonding agent strength agent 86-Λ C 3 strength debonding agent Milk U 51 J ~~ __ 〇r \ 4 & Bonding agent strength agent latex BU 37 5 Latex strength agent debonding agent 66 ^^-6 6 Strength agent latex debonding agent 67 Λ0 ^ _ Retention rate. For example, there is a minimum. As shown in the table, the order of addition of the chemical agent can affect the latex. For example, in samples 1 to 4, the debonding agent is the latex plus the previous home. 29 200300810

的混濁係數 乳膠併入纖維原料的能力方 ..^ 牝刀在此被證明。首先,由10%漂 曰干皮紙軟木紙漿纖維來製備一 +表衙纖維泥漿。此泥漿在一不列 顚粕砰機中粉碎5分鐘吏並 辰度爲h6%。然後,將泥 展稀釋至濃度爲0.33%。 然後’從紙漿中取出六份纖維原料樣本(體積赠‘ 一:3公!:)’並把它們分别放在1000如燒杯内。之後,將 Λ ς。/、〜 〃 4履(固體含量(依溶液重量)爲 •。)(传自 Dow Chemical,商標 “ m 桩# ^ i 冏琛DL-239”)加到各纖維原 科‘本中,添加量分 ^ 此外,一二氨基胺四級去 、、口 制(得自 Goldschmidt,商樟真 “ Δ ” “ Ν 知馬 Ar0surf pa-727”)和 p咖”聚丙烯酿胺暫時濕強度劑(亦作爲乾強度劑)也被 :到原料中,添加量分别爲16·5 lb/T和6 5 Ib/T。遑些添加 背J加到樣本中的添加順序,每樣太 节铋尽自不同,其順序如表三所 不。每添加劑與下個添加劑的添加時間相隔5分鐘。 一旦加入添加劑,用水將原料樣本稀釋成ι〇〇〇瓜丨。h 分鐘後,根據範例一所述之方法讓樣本通過自由測試器 (Freeness Tester)的網篩來過遽。然後,依範例一二所述者 來測量混濁値和留存百分率。結果如表三所示Haze coefficient The ability of latex to incorporate fiber raw materials.... The trowel is proven here. First, a + epidermal fiber slurry was prepared from 10% bleached dry cork pulp fibers. This slurry was crushed for 5 minutes in a line of slag meal slamming machine and the time was h6%. Then, the mud was diluted to a concentration of 0.33%. Then ‘take six samples of fiber material from the pulp (volume gift‘ one: 3 males! :) ’and place them in 1000 beakers, respectively. After that, Λ ς. / 、 ~ 〃 4 (solid content (according to the weight of the solution) is •.) (Passed from Dow Chemical, trademark "m Post # ^ i 冏 琛 DL-239") added to each fiber original family, the amount added In addition, a diaminoamine quaternary dehydration agent (obtained from Goldschmidt, Shang Zhangzhen "Δ" "N Shima Ar0surf pa-727") and p coffee "polypropylene amine temporary wet strength agent (also As a dry strength agent): It is also added to the raw materials, with the addition amounts of 16.5 lb / T and 6 5 Ib / T. The order of addition of some additions to the sample, each bismuth is different. The sequence is as shown in Table 3. The time between each additive and the next additive is 5 minutes. Once the additives are added, the raw material sample is diluted with water to ι〇〇〇〇〇 丨 After h minutes, according to the method described in Example 1. Pass the sample through a Freeness Tester screen. Then, measure the turbidity and retention percentage as described in Example 1 and 2. The results are shown in Table 3.

去鍵結劑 表三:樣杲 (%) 第一添加 乳膠Debonding agent Table 3: Sample (%) First addition latex

Ucky-2003 0220 -February 20, 2003 30 200300810 發明說明, 3 強度劑 去鍵結劑 乳膠 48 73 4 去键結i 強度劑 乳膠 55 68__ 5 乳膠 強度劑 去键結劑 ^ 55 68 ______ 6 1強度劑 乳膠 去鍵結劑 45 75 __—-- 如表所示’當利用一二氨基胺四級化合物時,化學劑的 添加順序對於混濁係數的影響並不會像範例二使用咪唑口林 四級去鍵結劑般大。 範例四 乳膠併入纖維原料的能力在此被證明。首先,由10〇/〇漂 白牛皮紙軟木紙漿纖維來製備一纖維泥槳。此泥漿在一不列 _粉碎機中粉砰5分鐘,使其固體濃度爲丨·6%。然後,將泥 漿稀釋至濃度爲0.33%。 然後’從紙漿中取出六份纖維原料樣本(體積9〇9 重量3公克)’並把它們分别放在1 燒杯内。之後,將 陰離子苯乙烯-丁二埽乳膠溶液(固體含量(依溶液重量)爲 0.5%)(得自Dow Chemica卜商標“DL 239”)加到各纖維原 料樣本中’添加量分料2()lb/T。此外,—四級脂肪酸三燒 烴胺醋去鍵結劑(得自Goldschmidt,商標名稱“ )和“!丨丙烯㈣暫時濕強度劑(亦作爲乾強 f劑)也被加到原料中,添加量分别爲165_和65_。 這些添加劑加到樣本中的添加順序’每樣本皆不同,其 如表四所示。每添加劑與下個添加劑的添如時間相隔:分; 一:旦加入添加劑,用水將原料樣本稀釋成_二里 刀益里後,根據範例一所述之方法讓^ ^^本通過自由測試器 31 200300810 發明說明 (Freeness Tester)的網篩來過 來測量混濁値和留存百分率 遽。然後,依範例一、二所述者 。結果如表四所示。Ucky-2003 0220 -February 20, 2003 30 200300810 Description of the invention, 3 strength agent debonding agent latex 48 73 4 debonding i strength agent latex 55 68__ 5 latex strength debonding agent ^ 55 68 ______ 6 1 strength agent Latex debonding agent 45 75 __ --- As shown in the table 'When using a diaminoamine quaternary compound, the effect of the order of addition of the chemical agent on the turbidity coefficient will not be the same as that of Example 2 As big as a bonding agent. Example 4 The ability of latex to incorporate fiber materials is demonstrated here. First, a fiber mud paddle was prepared from 100/0 white kraft softwood pulp fibers. This slurry was slammed in a pulverizer for 5 minutes to make its solid concentration 丨 · 6%. Then, the mud was diluted to a concentration of 0.33%. Then “take out six samples of fiber material (volume 109, weight 3 g) from the pulp” and place them in 1 beakers. Thereafter, an anionic styrene-butadiene latex solution (solid content (by weight of the solution) was 0.5%) (obtained from Dow Chemica brand "DL 239") was added to each fiber raw material sample 'addition amount 2 ( ) lb / T. In addition, the quaternary fatty acid trisalinyl amine vinegar debonding agent (available from Goldschmidt, trade names "" and "!"丨 Propylene 强度 temporary wet strength agent (also used as dry strength f agent) is also added to the raw materials, and the added amounts are 165_ and 65_, respectively. The order in which these additives are added to the sample is different for each sample, as shown in Table IV. The time between each additive and the next additive is as follows: points; one: once the additives are added, the raw material sample is diluted to _ Erli Daoyili with water, and the ^ ^^ passes the free tester according to the method described in Example 1. 31 200300810 A Freeness Tester screen came over to measure turbidity and percent retention. Then, as described in Examples 1 and 2. The results are shown in Table IV.

範例五 乳膠併入纖維原料的能力在此被證明。首先,由1〇%漂 白牛皮紙軟木紙漿纖維來製備'纖維泥漿。此泥漿在一不列 顚粉碎機中粉碎5分鐘’使其固體濃度爲16%。然後,將泥 漿稀釋至濃度爲0 33〇/〇。 然後,從紙漿中取出六份纖維原料樣本(體積9〇9 mi, 重量3公克),並把它們分别放在刪^燒杯内。之後,將 一 f離Γ苯乙歸_丁二婦乳膠溶液(固體含量(依溶液重量)爲 0.5%)(得自Dow Chemica卜商標“DL_239”)加到各纖維原 枓樣本中,添加量分别爲2〇lb/T。此外,—二燒基二甲基四 級去鍵結劑(得自Goldschmidt,商標名稱“ Vads〇ft 137”) 和聚丙烯酿胺暫時濕強度劑(亦作爲乾強度劑)也 被加到原料中’添加量分别爲16.51b/T和65旧丁。這些添 ,記避臓頁) 200300810 發明說明續頁 加劑加到樣本中的添加順序’每樣本皆不同^其順序如表五 所示。每添加劑與下個添加劑的添加時間相隔5分鐘。 一旦加入添加劑,用水將原料樣本稀釋成i〇〇〇 25 分鐘後’根據範例一所述之方法讓樣本通過自由測試器 (Freeness Teste〇的㈣來過遽。然後,依範例…二所述者 來測量混濁値和留存百分率。結果如表五所示。 表五:相 1本結果 樣本 ------ 第一添加 ΐ键結劑 第二添加 第三添加 混濁値 60 留存率 (%) 65 2 乳膠 去键結劑 強度劑 81 48 3_ 強度劑 去键結劑 乳膠 80 49 4 去鍵結劑 強度劑 乳膠 56 67 5 乳膠 強度劑 去鍵結劑 56 67 6 ^強度劑 乳膠 去鍵結劑 r 57 66 如上所示,化學劑的添加順序對乳膠留存在纖維上的比 率是有影響的。例如,樣本4和5就產生低的混濁係數。 範例六 乳膠併入纖維原料的能力在此被證明。首先,由1〇%漂 白牛皮紙軟木紙漿纖維來製備一纖維泥漿。此泥漿在一不列 頦粉碎機中粉碎5分鐘,使其固體濃度爲1.6%。然後,將泥 漿稀釋至濃度爲0.33%。 然後’從紙漿中取出四份纖維原料樣本(體積9〇9 m卜 重量3公克),並把它們分别放在1〇〇〇mi燒杯内。之後,將 一陰離子苯乙烯-丁二烯乳膠溶液(固體含量(依溶液重量)爲 0’5/〇)(得自Dow Chemica卜商標“DL 239”)加到各纖維原 :ky~20030220 -February 20, 2003 33 200300810Example 5 The ability of latex to incorporate fiber materials is demonstrated here. First, a 'fiber slurry' was prepared from 10% bleached white kraft softwood pulp fibers. This slurry was pulverized in a line of pulverizers for 5 minutes' to give a solid concentration of 16%. Then, the slurry was diluted to a concentration of 0 33 0/0. Then, take out six samples of fiber raw material (volume 109 mi, weight 3 grams) from the pulp, and place them in the beaker. After that, a f-benzene acetophenone-butadiene latex solution (solid content (depending on the weight of the solution) of 0.5%) (obtained from Dow Chemica brand "DL_239") was added to each fiber original tincture sample, and the amount was added. They are 20 lb / T. In addition, dialkyl dimethyl quaternary debonding agent (available from Goldschmidt, trade name "Vads 0ft 137") and polypropylene amine temporary wet strength agent (also used as dry strength agent) are also added to the raw materials. The amount of Chinese 'added was 16.51b / T and 65 dices. (Add these, avoid the title page) 200300810 Description of the invention continued page The order of adding agents to samples is different for each sample ^ The order is shown in Table 5. Each additive is separated from the next additive by 5 minutes. Once the additives have been added, the raw material sample is diluted to 1005 minutes with water. 'After passing the sample through a freeness tester (Freeness Teste 0) according to the method described in Example 1. Then, according to the example ... Measure the turbidity and retention percentage. The results are shown in Table 5. Table 5: Samples of the results of phase 1 ------ The first addition of thorium bonding agent the second addition of the third addition of turbidity thorium 60 Retention rate (%) 65 2 latex debonding agent strength agent 81 48 3_ strength agent debonding agent latex 80 49 4 debonding agent strength agent latex 56 67 5 latex strength debinding agent 56 67 6 ^ strength agent latex debonding agent r 57 66 As shown above, the order in which the chemicals are added has an effect on the ratio of latex remaining on the fibers. For example, samples 4 and 5 produce low turbidity coefficients. Example 6 The ability of latex to incorporate fiber raw materials is here Proof. First, a fibrous slurry was prepared from 10% bleached kraft softwood pulp fibers. This slurry was pulverized in a column grinder for 5 minutes to a solid concentration of 1.6%. Then, the slurry was diluted to a concentration of 0.3 3%. Then four samples of the fiber material (volume of 909 m and weight of 3 grams) were taken from the pulp and placed in a 1000-mi beaker. After that, an anionic styrene-butane Ethylene latex solution (solid content (based on solution weight) is 0'5 / 〇) (obtained from Dow Chemica, "DL 239") added to each fibrilogen: ky ~ 20030220 -February 20, 2003 33 200300810

料樣本中,添加量分别爲2〇 lb/T。 “此外,“Pr〇Soft TQ__”,“Ar〇謝f Μ 爪”, Vamoft We_16”和“Varis〇ft 137”分别被加到樣本卜4 十,其添加量分别爲16·5 lb/T。“ ,是一In the sample, the addition amount is 20 lb / T. "Furthermore," PrSoft TQ__ "," Ar〇 thank f M claw ", Vamoft We_16" and "Varis〇ft 137" were added to the sample BU 40 respectively, and the addition amounts were 16.5 lb / T. " ,is one

種聚氨環氧氯丙燒永久濕強度劑,亦可加到原料中,其添加 量爲8.5麟。這些添加劑的添加順序爲去鍵結劑,強度劑 和乳膠。每添加劑與下個添加劑的添加時間相隔5分鐘。 一且加入添加劑,用水將原料樣本稀釋成1〇〇〇爪卜乃 分鐘後,根據範例一所述之方法讓樣本通過自由測試器 (Freeness Tester)的網篩來過遽。然後,例—所述者來測 量混濁値和留存百分率。結果如表六所示。 樣本 厂-- 私,、•休令拜禾 去鍵結劑 混濁値 留存率(%) 1 Prosoft T(^1003(咪唑口林四級化合物、 20 1 4 1 \ χ ^ / 94 2 ArosmfPA727G^氨二胺四級化合物) 34 Q Λ 3 Vansoft --—-— Ο 4 鍵結劑) 24 91 4 Vansoft 137(二烷基二甲基四級化合物) 41 78This kind of polyurethane epoxychloropropene sintering permanent wet strength agent can also be added to the raw material, and its added amount is 8.5 Lin. These additives are added in the order of debonding agent, strength agent and latex. Each additive is separated from the next additive by 5 minutes. Once the additives were added, the raw material samples were diluted to 1,000 claws per minute with water, and then the samples were passed through a freeness tester screen according to the method described in Example 1. Then, use the example described to measure turbidity and retention. The results are shown in Table 6. Sample Plant-Private, • Xiuling Baihe Debonding Agent Clouding Retention Rate (%) 1 Prosoft T (^ 1003 (Quizolin 4th Compound, 20 1 4 1 \ χ ^ / 94 2 ArosmfPA727G ^ Ammonia Diamine quaternary compound) 34 Q Λ 3 Vansoft ------ 〇 4 bonding agent) 24 91 4 Vansoft 137 (dialkyldimethyl quaternary compound) 41 78

產生最低的混濁係數 範例七 形成只會產生少量脱落之柔軟薄紙的能力被證明。在一 造紙機器上產生九份薄紙樣本(樣本7-15),如第一圖及上面 所述。明確地説,形成了兩薄紙片,且此二薄紙片平貼在一 起而形成一單一薄片。然後,此單一薄片被壓縮,乾燥並起 縐。使用個别的原料槽來形成各分離薄紙片。原料槽的空氣 [3續次頁(發明說明頁不敷使用時,請註記並使用續頁) p K 〇 〇 ^ ~ ^ ^ ^ 8-Becky- 20030220 -February 20, 2003 34 200300810 發明說明續頁 側含有北方軟木牛皮紙纖維(LL_19,得自Kimberiyciark), 而乾燥側原料槽含有得自BahllSu.,Inc•的按屬植物纖維。在 :本HM5中’ LL-19纖維藉—位在原料槽下方的精鍊機精 鍊7分鐘。各樣本的基重爲每平方公尺3〇公克’且含有35% 的LL-19軟木纖維和65%的桉屬植物纖維。 在樣本 7-9 中,“ Kymene 557 LX” ,從贫- 工^、 LX (一種聚氨基環氧氣 丙乾水久濕強度劑)以4 lb/T的添加量被加到乾燥側原料槽 中’並以4 lb/T的添加量被加到空氣侧原料槽中。此外, “ P㈣’聚丙歸醯胺暫時濕強度劑(亦作爲乾強度劑)被加 到空氣側原料幫浦中,其添加量介於〇至3比邝之間。 在樣本10-12巾,“Kymene 557 Lx”以4 ib/T的添加 量被加到㈣側原料財’纽41b/T的量被㈣空氣例原 料槽中。將泥漿以15分鐘後,6lbs/T@黯⑽⑽ DC-i 83卜種咪㈣四級去鍵結劑,得自Meintym)亦被 加入乾燥側原料槽中。進一步地,“卩咖” &丙婦醯胺暫時 濕強度劑(亦作爲乾強度劑)亦被加到空氣側原料幫浦中,其 添加量介於〇至7·5 lb/T之間。 ^ 樣本13-15的形成方式與樣本1(M2相同,但另外添加 了 20 lbs/T的Airflex A_1〇5(一種乙歸基醋酸鹽乙歸共聚物 乳膠’得自Air* PrGduets)至空氣側原料槽中。進―步地, 聚丙埽酿胺暫時濕強度劑(亦作爲乾強度劑)也被 加到空氣側原料幫浦中,添加量分别爲2丨b/T和l〇ib/T。 成形心本的抗張強度,脱落和堅硬度則以下列方 式測定。 mrnmrnm) 200300810 發明說明$賣頁 1張強度 ~ ~ 抗張強度以“GMT”(每3英吋樣本多少公克)表示,它 是一種幾何平均抗張強度且以產品MD抗張強度和^〇抗= 強度的平方根來計算。MD和CD抗張強度使用Μτ_η_ 張力測試儀(得自 MTS Systems C〇rp.,Eden Praire,MN)來決 定。在機器方向和機器橫向上量出並剪下3英吋寬度的薄:氏Produces the lowest turbidity factor Example 7 The ability to form a soft tissue that produces only a small amount of shedding has been demonstrated. Nine tissue paper samples (samples 7-15) were produced on a paper machine, as described in the first figure and above. Specifically, two thin paper sheets are formed, and the two thin paper sheets are flatly adhered together to form a single sheet. This single sheet is then compressed, dried and creped. Individual stock tanks are used to form each separate tissue sheet. Air in the raw material tank [3 Continued pages (Please note and use continuation pages when the invention description page is insufficient.) P K 〇〇 ^ ~ ^ ^ ^ 8-Becky- 20030220 -February 20, 2003 34 200300810 Invention description continued page The side contains northern softwood kraft fiber (LL_19, available from Kimberiyciark), while the dry side raw material tank contains the plant fiber from Bahll Su., Inc •. In this HM5, the LL-19 fiber is borrowed from the refiner chain located under the raw material tank for 7 minutes. Each sample had a basis weight of 30 grams per square meter 'and contained 35% LL-19 softwood fibers and 65% eucalyptus fibers. In Samples 7-9, "Kymene 557 LX" was added to the dry side raw material tank from the lean-industrial, LX (a polyaminoepoxypropane dry water long-time wet strength agent) at an addition amount of 4 lb / T. 'And added to the air-side raw material tank with an addition amount of 4 lb / T. In addition, "P㈣'Polymeridamine's temporary wet strength agent (also used as a dry strength agent) was added to the air-side raw material pump in an amount of 0 to 3 ratios. In the sample 10-12 towels, "Kymene 557 Lx" was added to the raw material tank at the side of ㈣41b / T in an amount of 4 ib / T. The raw material tank was filled with air. After 15 minutes, the slurry was 6lbs / T @ an⑽⑽ DC- i 83-type Mimid (4th grade debonding agent, obtained from Meintym) is also added to the raw material tank on the dry side. Further, "卩 CA" & trimethoprim temporary wet strength agent (also used as a dry strength agent) It is also added to the air-side raw material pump, and its addition amount is between 0 and 7.5 lb / T. ^ Samples 13-15 are formed in the same way as sample 1 (M2, but an additional 20 lbs / T is added Airflex A_1〇5 (an ethylidene acetate ethylate copolymer latex 'from Air * PrGduets') into the air-side raw material tank. Further, polypropylene amine fermented temporary wet strength agent (also used as a dry strength agent) ) Is also added to the air-side raw material pump, with the addition amounts of 2 丨 b / T and 10b / T. The tensile strength, shedding and hardness of the shaped core are below Mrnmrnm) 200300810 Description of the invention $ 1 selling page strength ~ ~ The tensile strength is expressed as "GMT" (how many grams per 3 inch sample), it is a geometric mean tensile strength and is based on the MD tensile strength of the product and ^ 〇 Resistivity = Calculated as the square root of strength. MD and CD tensile strengths were determined using a Mτ_η_ Tensile Tester (available from MTS Systems Corp., Eden Praire, MN). Measure and cut in the machine direction and cross direction of the machine 3 inches wide thin:

樣本。在每次測試中,樣本被放在測試儀的鉗口中,而面紙 的範圍長度設4英忖,浴廁用紙則設2英叶。在測試期間, 通過前頭的速度爲1G in./mine測試儀與—下載有數據取得 系統(如供視窗軟體使用的MTS Testw叫的電腦連接。從電 腦螢幕上的斷點處直接讀値以獲得各樣本的抗張強度。电 脱落 1sample. In each test, the sample was placed in the jaws of the tester, the range of facial tissue was set to 4 inches, and the toilet paper was set to 2 inches. During the test, it is connected to a computer with a data acquisition system (such as MTS Testw for Windows software) through a tester with a speed of 1G in./mine in the front. Read directly from the breakpoint on the computer screen to obtain Tensile strength of each sample. Electrical shedding 1

――爲了決定纖維在織物上摩擦的的抗磨性或傾向,各樣 精者摩擦薄紙樣品而以下列方法來測量。此測試是測量薄^ 材料在—水平往復運動的磨石表面上作摩擦的抗磨性。所; 縣都在溫度2rc±rc和相對濕度5%±2%的情況下測試 分鐘,共測4小時。第四圖爲測試設備的圖示。 摩擦轴含有—直徑G 5”的不鏽鋼桿,其摩擦部份是t 〇蕭,深纟’ 4·25”長度的绩石圖案圍繞在桿的圓周上户“ 成摩擦軸係與儀器表面垂直而置,使桿的摩擦部份從儀含 表面向外延伸出整個長度。在摩擦軸的每一側設有一具御 紐的導引針,其一者可移動而另一者固定,彼此相隔4,且4 擦軸恰位在其中間。可移動的鉗和導引針可以以垂直方 由地滑動’而鉗口的重量確保樣本在摩擦軸表面能有———In order to determine the abrasion resistance or tendency of the fibers to rub on the fabric, each fine person rubs a tissue paper sample and measures it by the following method. This test measures the abrasion resistance of a thin material on the surface of a horizontally reciprocating grinding stone. All counties tested for 4 hours at a temperature of 2rc ± rc and a relative humidity of 5% ± 2%. The fourth figure is a diagram of the test equipment. The friction shaft contains a stainless steel rod with a diameter of 5 ”, the friction part of which is t 〇 Xiao, deep 的 4 · 25” length of the stone pattern around the circumference of the rod “to form a friction shaft system perpendicular to the surface of the instrument and So that the friction part of the rod extends from the instrument surface to the entire length. On each side of the friction shaft is a guide pin with a royal button, one of which can be moved and the other fixed, separated from each other 4 , And the 4 wiper shaft is exactly in the middle. The movable pliers and guide pin can slide in a vertical direction, and the weight of the jaw ensures that the sample can have on the surface of the friction shaft—

S3續次頁 PK001 -08 1 8-B 4¾¾¾請註記並使麵頁) 36 200300810 發明說明_胃 的張力。 ' 一·' -- 使用一具有模具切割器的模具壓機,裁剪出寬3,,土 ’〇5 X長8的長條,此長條在樣品兩端各具有2個洞。對薄 紙樣本來説,MD方向對應較長尺寸的那邊。然後,將各測 試長條秤重,最小單位爲〇 lmg。將樣本各端放到導引針上 且用磁性鉗來固定樣本。然後,讓可移動的鉗口掉下來通過 摩擦軸而形成穩定的張力。 —然後,把摩擦軸以與中央垂直線夾15度角的狀態,靠 著測試長條而以水平方向前後移動2〇圈(來回一次算一 圈),速度爲一分鐘80圈,把織物表面上鬆掉的纖維除去。 此外,摩擦軸以5 RPMs的轉速以順時鐘方向(當看著儀器前 側的時候的方向)旋轉。然後將磁性甜從樣本處移走且將樣本 從導引針上拿下來,並用壓縮空氣(5-1〇1)川來將樣本表面上 鬆掉的纖維吹走。然後秤重此測試樣本(最小單位爲〇3 mg),並記錄損失的重量。每種薄紙測試1〇個樣本,並以毫 克爲單位記綠平均損使的重量。 聖硬唐 間硬度(或柔軟度)的以〇至丨6的等級來評定,其中値越 低表示薄紙越柔軟而値越高表示薄紙越硬。要求12個參加 者當樣本他們手中時,評量樣本的尖端,波浪或破裂邊緣或 尖峰的感覺。讓參加者將放兩張薄紙樣本平放在一平滑桌面 上。此二樣本彼此重疊0.5英吋(1·27公分)且被翻轉,使得 測試期間薄紙樣本的相對側會呈現出來。各參加者利用他們 放在桌子上的前臂/肘邵,將手在樣本上打開,掌心向下。每 0續次頁 ρ Κ 00 1 -os 18-B e i發請註記雌臓頁) 37 200300810 發明說明It] 個人都會放著他們的手,讓 心分)的地方。各參加者將其手指小力地 他們溫和地將樣本移到掌心……乂…‘本。 各參加者對然後平均並記錄 ^ 考對薄、·、氏樣本的評定等級。 結果示於表七。S3 Continued page PK001 -08 1 8-B 4¾¾¾ Please note and make the face page) 36 200300810 Description of the invention _ stomach tension. '一 ·'-A die press with a die cutter was used to cut a strip with a width of 3, and a soil length of '05 × 8, which had two holes at each end of the sample. For thin paper samples, the MD direction corresponds to the longer dimension. Then, each test bar is weighed, and the minimum unit is 0.01 mg. Place each end of the sample on the guide pin and secure the sample with magnetic forceps. Then, let the movable jaw fall down and form a stable tension by rubbing the shaft. —Then, the friction axis is placed at a 15-degree angle from the central vertical line, and the test bar is moved horizontally back and forth by 20 turns (counting back and forth once) at a speed of 80 turns per minute. Loose fibers are removed. In addition, the friction shaft rotates in a clockwise direction (the direction when looking at the front of the instrument) at a speed of 5 RPMs. Then remove the magnetic sweet from the sample and remove the sample from the guide pin, and use compressed air (5-10) to blow loose fibers from the surface of the sample. The test sample was then weighed (the smallest unit was 0 3 mg) and the weight lost was recorded. Ten samples of each type of tissue paper were tested and the average weight loss in green was recorded in milligrams. The hardness (or softness) of the sacred hard Tang is evaluated on a scale of 0 to 6, where lower 値 indicates softer tissue and higher 値 indicates harder tissue. Twelve participants were asked to evaluate the sensation of the tip, wavy or cracked edges or spikes of the sample while the sample was in their hands. Ask participants to place two thin paper samples flat on a smooth table. The two samples overlap each other by 0.5 inch (1.27 cm) and are turned over so that the opposite side of the tissue paper sample appears during the test. Participants used their forearms / elbows on the table to open their hands on the samples with their palms down. Every 0 Continued pages ρ Κ 00 1 -os 18-B e i (please note the female page) 37 200300810 Description of the invention It] places where individuals put their hands and let their heart divide). Each participant put their fingers lightly. They gently moved the sample to the palm of their hands ... 乂 ... ‘this. Each participant then averaged and recorded ^ test the rating of thin, ·, and 、 samples. The results are shown in Table VII.

如表七所不的結果,本發明所添加的乳膠可以提供強 的柔軟的薄紙製品且產生較低量的脱落。As shown in Table 7, the latex added in the present invention can provide a strong soft tissue product with a lower amount of shedding.

範例八 形成柔軟且低量脱落之薄紙的能力在此被證明。三份薄 紙樣本(樣本16·18)依第三圖所示的方式被形成,但是用_張 以兩分離^平貼在—起_成的單_薄片㈣成未起續 的經乾燥薄紙,如第一圖所示。 柏紙的底片係由具有兩層的前頭匣所形成。具二層之前 頭厘的較低層含有得自Bahil Su·,Inc的桉屬植物纖維,而前 0續次頁Example 8 The ability to form soft, low-volume tissue paper is demonstrated here. Three tissue paper samples (samples 16 · 18) were formed as shown in the third figure, but _ sheets were separated in two ^ flatly attached to the _ formed single _ sheet into uncontinuous dried tissue paper, As shown in the first figure. The cypress paper is formed by a two-layer head box. Before the second layer The lower layer of the top contains the eucalyptus fiber from Bahil Su, Inc., and the first 0 continued pages

Ρ κοο 1 -0 8 I8-B 38 200300810 發明說明,續頁 頭E的較高層具有北方軟木牛皮紙纖維(ll i9,得自 Kimberly_Clark)。上部薄片係由得自%,心的按屬植 t纖維Γ形成。薄紙的各層具有自己的原料系統(包含原料 槽,記量幫浦,風扇幫浦和水流處理)各薄紙樣本的基重爲每 平方公尺30公克且含有40% LL_19軟木纖維和6〇%桉屬纖 維(各薄片相等)。 在樣本16中,4.5lb/T的“Parez”聚丙埽醯胺暫時濕強 度劑(亦作爲乾強度劑)和16 5 lb/T的Mackernium DC_i83(一 種米吐口林四級去鍵結劑,得自Mclntyre,W )被加到桉屬植 ^原料槽中,以供應雙層前頭E和上部薄片用。此外,8 lb” “ Parez”聚丙烯醯胺暫時濕強度劑(亦作爲乾強度劑)被加 到LL-19原料㈣卜使用位在原料槽下方的精鍊機來精鍊 LL-19纖維1〇分鐘。 以與製備樣本16相同的方法來製備樣本17,但當薄片 的固體濃度爲20%時,將1〇 lb/T的Airflex a1〇5(一種乙埽 基醋I鹽乙烯共聚物乳膠,得自Ak PrQduets)被喷灑到快速 輸送4和經全氣乾燥機(第三圖)之間較低的桉屬植物薄片層 上。使用一 Hl/8,,VV-SS65〇〇17VeeJet喷嘴(得自补咖叫 ystems, Inc·,位在 Milwaukee,Wisconsin)來將乳膠喷在薄Ρ κοο 1 -0 8 I8-B 38 200300810 Description of the invention, the upper layer of the continuation head E has northern softwood kraft fibers (lli9, available from Kimberly_Clark). The upper lamellae are formed from the centipede-derived t-fibers Γ. Each layer of tissue paper has its own raw material system (including raw material tank, metering pump, fan pump, and water flow treatment). The basis weight of each tissue paper sample is 30 grams per square meter and contains 40% LL_19 softwood fiber and 60% eucalyptus. Fiber (Each sheet is equal). In Sample 16, 4.5 lb / T of "Parez" polypropylene methamine temporarily wet strength agent (also used as a dry strength agent) and 16 5 lb / T of Mackernium DC_i83 (a kind of Mitoguline four-level debonding agent), Since Mclntyre, W) was added to the eucalyptus plant material tank to supply the double-layer front E and the upper sheet. In addition, 8 lb "" Parez "polypropylene ammonium temporary wet strength agent (also used as dry strength agent) was added to the LL-19 raw material. Using a refiner located under the raw material tank to refine the LL-19 fiber for 10 minutes Sample 17 was prepared in the same manner as Sample 16 except that when the solids concentration of the flakes was 20%, Airflex a105 (an ethyl acetate vinyl salt copolymer latex of 10 lb / T) was obtained. (From Ak PrQduets) was sprayed onto the lower eucalyptus sheet layer between the fast conveyer 4 and the full air dryer (third picture). Using a Hl / 8, VV-SS65〇17VeeJet nozzle (obtained Self-cooking coffee called ystems, Inc. (milwaukee, wisconsin) to spray latex on thin

片上。噴嘴以65度角的狀態將乳膠喷在薄片上,喷灑速度 爲每分鐘0.017加侖而壓力爲每平方英吋4〇磅。此外,6 lb/T 的“Parez”聚丙烯醯胺暫時濕強度劑(亦作乾強度劑)被加 到LL-19原料幫浦中。 “本1 8以與樣本1 7相同的方式來製備,但所使用的乳 ΰ續次頁 Ρ Κ00 1 -os]s^B ec (發明說明頁不敷使用時, ky-20030220 -February 20, 2003 請註記並使用續頁) 39 200300810 膠爲陰離必 ---二_ 稱爲“Γ:9”歸乳膠(得自D〇W 一^ 時濕、外,71b/T的“Parez”聚丙埽酿胺暫 “強度劑(亦作乾強度劑)被加到LL-19原料幫浦中。 強产成:^即可依範例七所述之方法來測定樣本的抗張 又脱洛軸況和間硬度。結果列於表八。 脱落 堅硬度 9.50 4.47 * 7.36 4.53 6.83 —---—-- _4.69 衣八a. The nozzle sprayed the latex onto the sheet at a 65-degree angle with a spray rate of 0.017 gallons per minute and a pressure of 40 pounds per square inch. In addition, a 6 lb / T "Parez" polypropylene amidamide temporary wet strength agent (also called a dry strength agent) was added to the LL-19 raw material pump. "The present 18 was prepared in the same manner as in the sample 17, but the lactation continuation sheet used was P CK00 1 -os] s ^ B ec (when the invention description sheet is insufficient, ky-20030220 -February 20, 2003 Please note and use the continuation sheet) 39 200300810 Glue is a must-have --- 2_ It is called "Γ: 9" latex (obtained from D〇W ^ hr wet, outside, 71b / T "Parez" polypropylene The "strengthening agent (also known as dry strength agent) is added to the LL-19 raw material pump. Strong production: ^ You can use the method described in Example 7 to determine the tensile and deloxation of the sample. And the hardness. The results are shown in Table 8. Shedding hardness 9.50 4.47 * 7.36 4.53 6.83 —------ _4.69 Yiba

的柔軟薄紙製品且產生較低量的脱落 ^在本發明以特定實施例詳細説明的同時,應瞭解熟於此 員技術者_旦瞭解前述内容後,可以輕㈣想出這些實施例 勺#換,交化物或同等物。所以本發明的範圍將由附加的 申4專利範園和其所有同等物來評定。 Θ續次頁 P K00 I -08I8-β 40 200300810 圖示元件簡單説明 1 first stock chest 第一原料槽 2 stock pump 原料幫浦 3 dilution water 稀釋水 4 fan pump 風扇幫浦 5 metering pump 計量會浦 6 headbox 前頭匣 7 papermaking fabric 造紙組織 8 sunction box 抽吸箱 11 second stock chest 第二原料槽 12 stock pump 原料幫浦 13 dilution water 稀釋水 14 fan pump 風扇幫浦 16 headbox 前頭匣 17 papermaking fabric 造紙組織 18 suction box 抽吸箱 19 roll 滾輪 20 vaccum box 眞空箱 22 felt 毛氈 30 dryer 乾燥機 31 pressure roll 壓力輪 32 roll 滾輪 41 layered headbox 分層前頭匣 42 forming fabric 成形組織 43 forming roll 成形滾輪 44 felt 造紙毛8¾ 45 press roll 壓輪 46 Yankee dryer 揚基乾燥機 47 creping doctor blade 起縐處理刮刀 110 papermaking headbox 造紙前頭匣 111 newly-formed wet web 新成形的濕織物 112 upper forming fabric 上成形組織 113 lower forming fabric 較低的成形組織 117 transfer fabric 輸送組織 119 through-drying fabric 經乾燥組織 121 through - dryer 經乾燥機 140 spray nozzle 噴嘴 □續次頁(發明說明頁不敷使用時,請註記並使用續頁) PK001-0818-Becky-20030220 -February 20, 2003 4 1Soft tissue products with lower amount of shedding ^ While the present invention is described in detail with specific embodiments, it should be understood by those skilled in the art_ Once you understand the foregoing, you can tap out these embodiments , Cross compound or equivalent. Therefore, the scope of the present invention will be evaluated by the additional patent application park and all equivalents thereof. Θ Continued page P K00 I -08I8-β 40 200300810 Brief description of the components in the diagram 1 first stock chest First raw material tank 2 stock pump Raw material pump 3 Dilution water 4 fan pump Fan pump 5 metering pump 量 会 浦 6 headbox front paper box 7 papermaking fabric papermaking organization 8 sunction box suction box 11 second stock chest second raw material tank 12 stock pump raw material pump 13 dilution water dilution water 14 fan pump fan pump 16 headbox front paper box 17 papermaking fabric papermaking organization 18 suction box suction box 19 roll roller 20 vaccum box empty box 22 felt felt 30 dryer dryer 31 pressure roll pressure roller 32 roll roller 41 layered headbox layered front head box 42 forming fabric forming tissue 43 forming roll 44 felt papermaking wool 8¾ 45 press roll 46 Yankee dryer Yankee dryer 47 creping doctor blade 110 creping doctor blade 110 papermaking headbox 111 newly-formed wet web 112 upper forming fabric 113 lower forming fabric Low forming structure 117 transfer fabric 119 through-drying fabric 121 through-dryer 140 through nozzle 140 spray nozzle Nozzle □ Continued (If the description page of the invention is insufficient, please note and use the continued page) PK001- 0818-Becky-20030220 -February 20, 2003 4 1

Claims (1)

200300810 申請專利範圍續頁 拾、申請專利範圍 1 · 一種形成薄紙製品的方法,其包含: 提供一纖維素纖維的液體原料; 以該纖維素纖維的液體原料形成一多層濕織物; 添加一去键結劑至該原料,該濕織物或它們的組合物 中; 添加至少一破璃過渡溫度少於3 01〇的乳膠至該液體原 料,該濕織物或它們的組合物中,該乳膠的添加量少於每, 該纖維素纖維乾重60镑;以及 乾燥該濕織物,其中該乾燥織物的至少一外層包含該 經乳膠處理的纖維素纖維。 2. 如申請專利範園第1項所述之方法,其中該乳膠的破璃 過渡溫度大於-25¾。 3 · 如申請專利範圍第1項所述之方法,其中該乳膠的破璃 過渡溫度介於-15¾至15°C之間。 4· 如申請專利範圍第1項所述之方法,其中該乳膠的坡璃 過渡溫度介於-1010至〇 eC之間。 5 · 如申請專利範園第1項所述之方法,其中該乳膠係選自 含有苯乙埽-丁二埽共聚物,聚乙埽基醋酸鹽同相聚合物, 乙埽基··醋酸鹽乙埽共聚物,乙婦基-醋酸鹽丙烯酸共聚物, 乙烯-乙烯基氯化物共聚物,乙烯-乙烯基氣化物-乙烯基醋酸 鹽三聚合物,丙烯酸聚乙烯氯化物聚合物,丙烯酸聚合物和 亞硝酸聚合物所組成的基團。 (3續次頁(發明說明頁不敷使用時,請註記並使用續頁) p κ 0 〇 I - 〇 8 1 8 - B e c ky - 2 0 0 3 0 2 2 0 -February 20, 2003 42 200300810 申請專利範圍續頁 6. 如申請專利範園第1項所述之方法,其中該乳膠的添加 量爲每噸纖維素纖維乾重1多40碎。 7. 如申請專利範園第丨項所述之方珐,其中該乳膠的添加 量爲每噸纖維素纖維乾重1裏2〇時。 8 ·如申請專利範圍第1項所述之方祛,其中該去鍵結劑係 添加在該乳膠之前。 9 · 如申請專利範圍第1項所述之方法,其進一步包含添加 一濕強度劑至該原料,該濕織物或它們的組合物中。 I 0.如申請專利範園第9項所述之方法,其中該濕強度劑係 添加在該乳膠之前。 II ·如申請專利範圍第9項所述之方法,其中該濕強度劑包 括一暫時濕強度劑。 12·如申請專利範圍第π項所述之方法,其中該暫時濕強 度劑包含一陽離子聚丙烯醯胺聚合物。 1 3 ·如申請專利範園第1 1項所述之方珐,其中該暫時濕強 度劑的添加量爲每,該纖維素纖維乾重1至60磅。 14 ·如申請專利範園第9項所述之方法,其中該濕強度劑包 括一永久濕強度劑。 1 5 ·如申請專利範園第14項所述之方珐,其中該永久濕強 度劑包含一陽離子聚氨聚合物。 16.如申請專利範圍第14項所述之方法,其中該永久濕強 度劑的添加量爲每噸該纖維素纖維乾重1至20磅。 1 7 ·如申請專利範圍第1項所述之方法,其中該去键結劑包 括一咪唑叫四級化合物。 Ξ續次頁 PK001-0818-Bec (發明說明頁不敷使用時,請註記並使用續頁) ^20030220 -February 20, 2003 43 200300810 __ 申請專利範圍$買頁 18.如申請專利範圍第1項所述之方法,其中該去鍵結劑包 括一醋官能基四級銨化合物。 1 9 ·如申請專利範圍第1項所述之方法,其中該去鍵結劑的 添加量爲每噸該纖維素纖維乾重1至3 0磅。 20·如申請專利範圍第1項所述之方法,其中該乳膠有60% 以上的量留存在該纖維素纖維上。 2 1 ·如申請專利範圍第1項所述之方珐,其中該乳膠有75% 到90%的量留存在該纖維素纖維上。 22·如申請專利範圍第1項所述之方法,其中該乳膠係被喷 灑至該濕織物上。 23. —種形成薄紙製品的方法,其包含: 提供一纖維素纖維的液體原料; 以該纖維素纖維的液體原料形成一多層濕織物; 添加一去鍵結劑至該原料,該濕織物,或它們的組合 物’該去鍵結劑的添加量爲每噸該纖維素纖維乾重1至3〇 磅; 添加一濕強度劑至該原料,該濕織物或它們的組合物, 该濕強度劑係選自暫時濕強度劑,永久濕強度劑和它們的組 合物所組成的基團; 添加至少一乳膠至該原料,該濕織物或它們的組合物, 該乳膠的添加量爲每噸該纖維素纖維乾重1至40磅,該乳 膠的玻璃過渡溫度少於3〇〇c且大於_25亡;以及 乾燥1¾濕織物,其中該乾燥織物的至少一外層含有該經 乳膠處理的纖維素纖維。 [3續次頁 P K00 1 -0818-Bec (發明說明頁不敷使用時, ky-20030220 -February 20, 2003 請註記並使用續頁) 44 200300810 申請專利範圍續頁 2 4 ·如申請專利範圍第2 3項所述之方法’其中该乳膠的玻 璃過渡溫度介於-15¾至15。〇之間。 2 5 ·如申請專利範園第2 3項所述之方法’其中该乳膠的玻 璃過渡溫度介於-10¾至〇。〇之間。 26. 如申請專利範圍第23項所述之方法,其中該乳膠係選 自含有苯乙烯·丁二烯共聚物,聚乙烯基醋酸鹽同相聚合 物,乙烯基-醋酸鹽乙埽共聚物,乙埽基-醋酸鹽丙烯酸共聚 物,乙埽-乙烯基氣化物共聚物,乙烯-乙烯基氣化物-乙烯基 醋酸鹽三聚合物,丙烯酸聚乙烯氯化物聚合物,丙埽酸聚合 物和亞硝酸聚合物所組成的基圈。 27. 如申請專利範圍第23項所述之方法,其中該去鍵結劑 係添加在該乳膠之前。 28·如申請專利範圍第23項所述之方法,其中該濕強度劑 係添加在該乳膠之前。 29.如申請專利範圍第23項所述之方法,其中該乳膠有 60%以上的量留存在該纖維素纖維上。 30·如申請專利範園第23項所述之方法,其中該乳膠有 75%至90%的量留存在該纖維素纖維上。 3 1.如申請專利範圍第23項所述之方法,其中該乳膠係被 喷灑到該濕織物上。 32·如申請專利範園第23項所述之方法,其中該乳膠的添 加量爲每噸纖維素纖維乾重1至20磅。 33· —種薄紙製品,其基重少於每平方公尺8〇公克,該薄 紙製品包含一多層紙類織物,其具有至少一界定出薄紙製品 囟續次頁 PK00I-0818-Bec (發明說明頁不敷使用時,請註記並使用續頁) ky-2〇〇3〇220 -February 20, 2003 45 200300810 申請專利範圍糸買頁 之一外部表面的外層,該外層係由纖維素纖維所形成,該纖 維素纖維添加有一去鍵結劑,一濕強度劑,以及至少一乳 膠,該乳膠的玻璃過渡溫度少於3〇亡且大於-25¾,該乳膠 的含量少於該外層乾重的3 %。 34.如申請專利範圍第33項所述的薄紙製品,其中該乳膠 含量爲該外層乾重的〇.〇5%至2%。 3 5.如申請專利範園第3 3項所述的薄紙製品,其中該乳膠 含量爲該外層乾重的〇·〇5%至1%。 3 6·如申凊專利範圍第3 3項所述的薄紙製品,其中該乳膠 的玻璃過渡溫度介於-15它至15 °C之間。 3 7 ·如申凊專利範園第3 3項所述的薄紙製品,其中該乳膠 的玻璃過渡溫度介於-1 〇 t至〇 IQ之間。 38·如申請專利範圍第33項所述的薄紙製品,其中該多層 酯類織物的其他層大體上不含該乳膠。 39· —種面紙,其係依申請專利範圍第33項所界定者。 40. —種浴廁用紙,其係依申請專利範圍第33項所界定者。 41·如申請專利範園第4〇項所述的浴廁用紙,其中該濕強 度劑本質上是由暫時濕強度劑所組成。 42. 一種紙巾’其係依申請專利範圍第33項所界定者。 43 · 一種薄紙製品,其基重少於每平方公尺8〇公克,該薄 紙製品包含一多層紙類織物,其具有至少一界定出薄紙製品 之一外邛表面的外層,該外層係由纖維素纖維所形成,該纖 維素纖維添加有一去鍵結劑,一濕強度劑,以及至少一乳 膠,該乳膠的玻璃過渡溫度少於3〇〇c而大於_25艺,該乳膠 200300810 ——-——___ 申請專利範圍續頁 含量少於薄紙製品的3 %。 44.如申請專利範圍第43項所述的薄紙製 含量爲該外層乾重的0.05%至2%。 45. 如申請專利範圍第4 3項所述的薄紙製品 含量爲該外層乾重的0.05%至1%。 46. 如申請專利範圍第43項所述的薄紙製品 的玻璃過渡溫度介於-15¾至15¾之間。 47. 如申請專利範圍第43項所述的薄紙製品 的玻璃過渡溫度介於-1 〇。<0至〇。<0之間。 其中該乳膠 其中讀乳膠 其中讀乳膠 其中該乳膠200300810 Scope of Patent Application Continued, Patent Application Scope 1 · A method for forming tissue paper products, comprising: providing a liquid raw material of cellulose fiber; forming a multilayer wet fabric from the liquid raw material of cellulose fiber; A bonding agent to the raw material, the wet fabric or their composition; adding at least one latex having a glass-breaking transition temperature of less than 301 to the liquid raw material, the wet fabric or their composition, the addition of the latex In an amount less than 60 pounds per dry weight of cellulose fibers; and drying the wet fabric, wherein at least one outer layer of the dried fabric comprises the latex-treated cellulose fibers. 2. The method according to item 1 of the patent application park, wherein the glass transition temperature of the latex is greater than -25¾. 3. The method according to item 1 of the scope of patent application, wherein the latex has a glass transition temperature between -15¾ and 15 ° C. 4. The method according to item 1 of the scope of patent application, wherein the latex has a slope transition temperature between -1010 and 0 eC. 5. The method according to item 1 of the patent application park, wherein the latex is selected from the group consisting of phenethylfluorene-butadiene copolymer, polyethyleneacetate homophase polymer, ethylacetate · acetate B Fluorene copolymer, ethynyl-acetate acrylic copolymer, ethylene-vinyl chloride copolymer, ethylene-vinyl gaseous-vinyl acetate terpolymer, acrylic polyvinyl chloride polymer, acrylic polymer and A group of nitrous acid polymers. (3 continuation pages (please note and use continuation pages when the invention description page is insufficient) p κ 0 〇I-〇8 1 8-B ec ky-2 0 0 3 0 2 2 0 -February 20, 2003 42 200300810 Scope of Patent Application Continued 6. The method described in item 1 of the patent application park, wherein the added amount of the latex is 1 to 40 pieces per ton of cellulose fiber dry weight. The said square enamel, wherein the added amount of the latex is 1 mile per 20 tons of dry weight of cellulose fiber. 8 · The formula described in item 1 of the patent application scope, wherein the debonding agent is added in Before the latex. 9. The method as described in item 1 of the scope of patent application, further comprising adding a wet strength agent to the raw material, the wet fabric, or a combination thereof. I 0. As claimed in Patent Application Park No. 9 The method according to item 1, wherein the wet strength agent is added before the latex. II. The method according to item 9 of the scope of patent application, wherein the wet strength agent includes a temporary wet strength agent. 12. The scope of patent application The method of item π, wherein the temporary wet strength agent comprises a cationic polypropylene Ammonium polymer. 1 3. The square enamel according to item 11 of the patent application park, wherein the temporary wet strength agent is added in an amount of 1 to 60 pounds per cell dry weight of the cellulose fiber. 14 · as applied The method according to item 9 of the patent model, wherein the wet strength agent comprises a permanent wet strength agent. 1 5 · The square enamel according to the item 14 of the application for the patent model, wherein the permanent wet strength agent comprises a cationic polymer Ammonia polymer. 16. The method according to item 14 of the scope of the patent application, wherein the permanent wet strength agent is added in an amount of 1 to 20 pounds per ton of the cellulose fiber dry weight. The method described in the above item, wherein the debonding agent includes an imidazole called a quaternary compound. Ξ Continued on the next page PK001-0818-Bec (When the description page of the invention is insufficient, please note and use the continuation page) ^ 20030220 -February 20 , 2003 43 200300810 __ Patent application scope $ buy page 18. The method as described in item 1 of the patent application scope, wherein the debonding agent includes a monofunctional quaternary ammonium compound. 1 9. The method according to the item, wherein the debonding agent is added The amount is 1 to 30 pounds of dry weight of the cellulose fiber per ton. 20. The method according to item 1 of the scope of patent application, wherein more than 60% of the latex is left on the cellulose fiber. 2 1 · The square enamel according to item 1 of the patent application scope, wherein 75% to 90% of the latex remains on the cellulose fiber. 22. The method according to item 1 of the patent application scope, wherein the latex is Sprayed onto the wet fabric. 23. A method for forming a tissue product, comprising: providing a liquid raw material of cellulose fibers; forming a multilayer wet fabric from the liquid raw material of cellulose fibers; adding a debonding agent to the raw material, the wet fabric Or their composition, the debonding agent is added in an amount of 1 to 30 pounds per ton of dry weight of the cellulose fiber; a wet strength agent is added to the raw material, the wet fabric or their composition, the wet The strength agent is selected from the group consisting of temporary wet strength agent, permanent wet strength agent and their composition; adding at least one latex to the raw material, the wet fabric or their composition, and the addition amount of the latex is per ton The cellulose fiber has a dry weight of 1 to 40 pounds, the latex has a glass transition temperature of less than 300c and is greater than -25 ° C; and a dry 1¾ wet fabric, wherein at least one outer layer of the dry fabric contains the latex-treated fiber Plain fiber. [3 Continued pages P K00 1 -0818-Bec (When the description page of the invention is insufficient, ky-20030220 -February 20, 2003 Please note and use the continuation page) 44 200300810 Scope of Patent Application Continued 2 4 · If the scope of Patent Application The method according to item 23, wherein the latex has a glass transition temperature of -15¾ to 15. 〇between. 25. The method according to item 23 of the patent application park ', wherein the glass transition temperature of the latex is from -10¾ to 0. 〇between. 26. The method as described in item 23 of the scope of patent application, wherein the latex is selected from the group consisting of styrene-butadiene copolymer, polyvinyl acetate homopolymer, vinyl-acetic acid ethyl acetate copolymer, ethyl acetate Ammonium-acetate acrylic acid copolymer, acetamidine-vinyl gaseous copolymer, ethylene-vinyl gaseous-vinyl acetate terpolymer, acrylic polyvinyl chloride polymer, propionic acid polymer and nitrous acid Base ring made of polymer. 27. The method of claim 23, wherein the debonding agent is added before the latex. 28. The method of claim 23, wherein the wet strength agent is added before the latex. 29. The method according to item 23 of the scope of patent application, wherein more than 60% of the latex is retained on the cellulose fibers. 30. The method according to item 23 of the patent application park, wherein 75% to 90% of the latex remains on the cellulose fibers. 3 1. The method according to item 23 of the scope of patent application, wherein the latex is sprayed onto the wet fabric. 32. The method according to item 23 of the patent application park, wherein the latex is added in an amount of 1 to 20 pounds per ton of cellulose fiber dry weight. 33 · A tissue product having a basis weight of less than 80 grams per square meter. The tissue product includes a multilayer paper fabric having at least one defining tissue product. Continued page PK00I-0818-Bec (Invention When the instruction sheet is not enough, please note and use the continuation sheet) ky-2〇〇〇2〇220 -February 20, 2003 45 200300810 Scope of patent application: One of the outer surface of the purchase page, the outer layer is made of cellulose fiber Formed, the cellulose fiber is added with a debonding agent, a wet strength agent, and at least one latex. The latex has a glass transition temperature of less than 30 ° C and greater than -25¾, and the content of the latex is less than the dry weight of the outer layer. 3%. 34. The tissue paper product according to item 33 of the scope of patent application, wherein the latex content is 0.05% to 2% of the dry weight of the outer layer. 3 5. The tissue paper product according to item 33 of the patent application park, wherein the latex content is 0.05% to 1% of the dry weight of the outer layer. 36. The tissue paper product as described in item 33 of the patent scope of Shenyang, wherein the glass transition temperature of the latex is between -15 ° C and 15 ° C. 37. The tissue paper product according to item 33 of Shenyang Patent Fanyuan, wherein the glass transition temperature of the latex is between -10 and 0 IQ. 38. The tissue product according to item 33 of the application, wherein the other layers of the multilayered ester fabric are substantially free of the latex. 39 · —Graft paper, as defined in item 33 of the scope of patent application. 40. A kind of toilet paper, as defined in item 33 of the scope of patent application. 41. The toilet paper according to item 40 of the patent application park, wherein the wet strength agent is essentially composed of a temporary wet strength agent. 42. A paper towel 'is defined in accordance with item 33 of the scope of patent application. 43. A tissue product having a basis weight of less than 80 grams per square meter. The tissue product includes a multilayer paper fabric having at least one outer layer defining an outer surface of one of the tissue products. The outer layer is made of It is formed by cellulose fibers. The cellulose fibers are added with a debonding agent, a wet strength agent, and at least one latex. The glass transition temperature of the latex is less than 300c and greater than _25. -——___ The scope of patent application for continuation pages is less than 3% of tissue paper products. 44. The content of tissue paper according to item 43 of the scope of patent application is 0.05% to 2% of the dry weight of the outer layer. 45. The content of the tissue paper product as described in item 43 of the scope of patent application is 0.05% to 1% of the dry weight of the outer layer. 46. The glass transition temperature of tissue paper products described in item 43 of the scope of patent application is between -15¾ and 15¾. 47. The glass transition temperature of tissue paper products as described in item 43 of the scope of patent application is between -10. < 0 to 0. < 0. Where the latex where read latex where read latex where the latex [□續次頁(發明說明頁不敷使用時,請註記並使用續頁) PK001-0818-Becky-20030220 -February 20, 2003 47[□ Continued pages (If the description page of the invention is insufficient, please note and use the continued pages) PK001-0818-Becky-20030220 -February 20, 2003 47
TW091134263A 2001-12-03 2002-11-26 Tissue products having reduced lint and slough TW200300810A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US10/005,882 US20030121627A1 (en) 2001-12-03 2001-12-03 Tissue products having reduced lint and slough

Publications (1)

Publication Number Publication Date
TW200300810A true TW200300810A (en) 2003-06-16

Family

ID=21718188

Family Applications (1)

Application Number Title Priority Date Filing Date
TW091134263A TW200300810A (en) 2001-12-03 2002-11-26 Tissue products having reduced lint and slough

Country Status (4)

Country Link
US (1) US20030121627A1 (en)
AU (1) AU2002349921A1 (en)
TW (1) TW200300810A (en)
WO (1) WO2003048453A1 (en)

Families Citing this family (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040043200A1 (en) * 2002-08-28 2004-03-04 Masek Jan K. Pliable paper
US7189307B2 (en) 2003-09-02 2007-03-13 Kimberly-Clark Worldwide, Inc. Low odor binders curable at room temperature
KR101087339B1 (en) 2003-09-02 2011-11-25 킴벌리-클라크 월드와이드, 인크. Low odor binder curable at room temperature
US6991706B2 (en) * 2003-09-02 2006-01-31 Kimberly-Clark Worldwide, Inc. Clothlike pattern densified web
US20050045293A1 (en) 2003-09-02 2005-03-03 Hermans Michael Alan Paper sheet having high absorbent capacity and delayed wet-out
US20050148261A1 (en) * 2003-12-30 2005-07-07 Kimberly-Clark Worldwide, Inc. Nonwoven webs having reduced lint and slough
JP4759933B2 (en) * 2004-04-26 2011-08-31 富士ゼロックス株式会社 Electrophotographic transfer paper and image forming method
US7297231B2 (en) * 2004-07-15 2007-11-20 Kimberly-Clark Worldwide, Inc. Binders curable at room temperature with low blocking
US7676088B2 (en) * 2004-12-23 2010-03-09 Asml Netherlands B.V. Imprint lithography
US20060144536A1 (en) * 2004-12-30 2006-07-06 Nickel Deborah J Soft and durable tissues made with thermoplastic polymer complexes
US20060144541A1 (en) * 2004-12-30 2006-07-06 Deborah Joy Nickel Softening agent pre-treated fibers
US7879188B2 (en) 2005-12-15 2011-02-01 Kimberly-Clark Worldwide, Inc. Additive compositions for treating various base sheets
US7842163B2 (en) * 2005-12-15 2010-11-30 Kimberly-Clark Worldwide, Inc. Embossed tissue products
US7879191B2 (en) 2005-12-15 2011-02-01 Kimberly-Clark Worldwide, Inc. Wiping products having enhanced cleaning abilities
US7883604B2 (en) 2005-12-15 2011-02-08 Kimberly-Clark Worldwide, Inc. Creping process and products made therefrom
US8444811B2 (en) 2005-12-15 2013-05-21 Kimberly-Clark Worldwide, Inc. Process for increasing the basis weight of sheet materials
US7837831B2 (en) 2005-12-15 2010-11-23 Kimberly-Clark Worldwide, Inc. Tissue products containing a polymer dispersion
US7879189B2 (en) 2005-12-15 2011-02-01 Kimberly-Clark Worldwide, Inc. Additive compositions for treating various base sheets
US7820010B2 (en) 2005-12-15 2010-10-26 Kimberly-Clark Worldwide, Inc. Treated tissue products having increased strength
US7807023B2 (en) 2005-12-15 2010-10-05 Kimberly-Clark Worldwide, Inc. Process for increasing the basis weight of sheet materials
WO2008156454A1 (en) 2007-06-21 2008-12-24 Kimberly-Clark Worldwide, Inc. Wiping products having enhanced oil absorbency
US7785443B2 (en) 2006-12-07 2010-08-31 Kimberly-Clark Worldwide, Inc. Process for producing tissue products
US7588662B2 (en) 2007-03-22 2009-09-15 Kimberly-Clark Worldwide, Inc. Tissue products containing non-fibrous polymeric surface structures and a topically-applied softening composition
US8105463B2 (en) 2009-03-20 2012-01-31 Kimberly-Clark Worldwide, Inc. Creped tissue sheets treated with an additive composition according to a pattern
US8282777B2 (en) * 2009-03-30 2012-10-09 Sellars Absorbent Materials, Inc. Disposable wipers and towels containing 40% or more post-consumer waste
US8894813B2 (en) 2012-08-17 2014-11-25 Kimberly-Clark Worldwide, Inc. Absorbent barrier tissue
US20140050890A1 (en) 2012-08-17 2014-02-20 Kenneth John Zwick High Basis Weight Tissue with Low Slough
US9283730B2 (en) 2012-08-17 2016-03-15 Kimberly-Clark Worldwide, Inc. High basis weight creped tissue
US8916025B2 (en) 2013-03-12 2014-12-23 Sellars Absorbent Materials, Inc. Disposable wipers and towels containing 100% recycled fibers
AU2015387523B2 (en) 2015-03-20 2020-06-25 Kimberly-Clark Worldwide, Inc. A soft high basis weight tissue
US11035078B2 (en) 2018-03-07 2021-06-15 Gpcp Ip Holdings Llc Low lint multi-ply paper products having a first stratified base sheet and a second stratified base sheet
CA3034832A1 (en) 2018-03-07 2019-09-07 Gpcp Ip Holdings Llc Low lint paper products and methods of making the same
WO2019209323A1 (en) * 2018-04-27 2019-10-31 Kimberly-Clark Worldwide, Inc. Durable tissue product

Family Cites Families (100)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
LU29095A1 (en) * 1942-07-31
US2745744A (en) * 1951-02-09 1956-05-15 Permacel Tape Corp Treating agents incorporation
US2926154A (en) * 1957-09-05 1960-02-23 Hercules Powder Co Ltd Cationic thermosetting polyamide-epichlorohydrin resins and process of making same
NL110447C (en) * 1957-09-05
US3104198A (en) * 1959-10-20 1963-09-17 Union Carbide Corp Papers with improved absorbent properties
US3256138A (en) * 1965-02-08 1966-06-14 John A Manning Paper Co Inc Application of resin particles to a wet fibrous ply in forming a multi-ply water-laid web
US3556932A (en) * 1965-07-12 1971-01-19 American Cyanamid Co Water-soluble,ionic,glyoxylated,vinylamide,wet-strength resin and paper made therewith
US3556933A (en) * 1969-04-02 1971-01-19 American Cyanamid Co Regeneration of aged-deteriorated wet strength resins
US3591529A (en) * 1970-02-02 1971-07-06 Nat Starch Chem Corp Phophorus-containing polyamines
US4208459A (en) * 1970-04-13 1980-06-17 Becker Henry E Bonded, differentially creped, fibrous webs and method and apparatus for making same
CA978465A (en) * 1970-04-13 1975-11-25 Scott Paper Company Fibrous sheet material and method and apparatus for forming same
US3700623A (en) * 1970-04-22 1972-10-24 Hercules Inc Reaction products of epihalohydrin and polymers of diallylamine and their use in paper
US3695985A (en) * 1970-07-29 1972-10-03 Kimberly Clark Co High bulk laminates
US3844880A (en) * 1971-01-21 1974-10-29 Scott Paper Co Sequential addition of a cationic debonder, resin and deposition aid to a cellulosic fibrous slurry
US3812000A (en) * 1971-06-24 1974-05-21 Scott Paper Co Soft,absorbent,fibrous,sheet material formed by avoiding mechanical compression of the elastomer containing fiber furnished until the sheet is at least 80%dry
US3862877A (en) * 1972-05-22 1975-01-28 Buckeye Cellulose Corp Clothlike tissue laminates
US3821068A (en) * 1972-10-17 1974-06-28 Scott Paper Co Soft,absorbent,fibrous,sheet material formed by avoiding mechanical compression of the fiber furnish until the sheet is at least 80% dry
US3879257A (en) * 1973-04-30 1975-04-22 Scott Paper Co Absorbent unitary laminate-like fibrous webs and method for producing them
US3903342A (en) * 1973-04-30 1975-09-02 Scott Paper Co Soft, absorbent, unitary, laminate-like fibrous web with delaminating strength and method for producing it
US4326000A (en) * 1973-04-30 1982-04-20 Scott Paper Company Soft, absorbent, unitary, laminate-like fibrous web
NL7308406A (en) * 1973-06-18 1974-12-20
US3885158A (en) * 1973-10-23 1975-05-20 Harris Corp Specimen block and specimen block holder
US4147586A (en) * 1974-09-14 1979-04-03 Monsanto Company Cellulosic paper containing the reaction product of a dihaloalkane alkylene diamine adduct and epihalohydrin
US4121966A (en) * 1975-02-13 1978-10-24 Mitsubishi Paper Mills, Ltd. Method for producing fibrous sheet
US4094717A (en) * 1975-06-03 1978-06-13 Aai Corporation Method of assembly of an insulating panel arrangement
US4099913A (en) * 1976-03-25 1978-07-11 Union Carbide Corporation Foams for treating fabrics
NO762394L (en) * 1976-07-16 1977-01-18 Aku Goodrich Chem Ind
US4222921A (en) * 1978-06-19 1980-09-16 Monsanto Company Polyamine/epihalohydrin reaction products
US4507173A (en) * 1980-08-29 1985-03-26 James River-Norwalk, Inc. Pattern bonding and creping of fibrous products
US4392861A (en) * 1980-10-14 1983-07-12 Johnson & Johnson Baby Products Company Two-ply fibrous facing material
US4441962A (en) * 1980-10-15 1984-04-10 The Procter & Gamble Company Soft, absorbent tissue paper
US4351699A (en) * 1980-10-15 1982-09-28 The Procter & Gamble Company Soft, absorbent tissue paper
US4510019A (en) * 1981-05-12 1985-04-09 Papeteries De Jeand'heurs Latex containing papers
FR2519663B2 (en) * 1981-05-12 1985-08-16 Jeandheurs Papeteries IMPROVEMENTS IN THE PROCESS FOR THE MANUFACTURE IN AQUEOUS MEDIA OF LEAVES OF FIBROUS MATERIALS CONTAINING LATEX OR THE LIKE AND / OR PHENOPLASTS OR AMINOPLASTS, NEW SHEETS THUS OBTAINED AND THEIR REUSE
US4447294A (en) * 1981-12-30 1984-05-08 The Procter & Gamble Company Process for making absorbent tissue paper with high wet strength and low dry strength
US5102501A (en) * 1982-08-18 1992-04-07 James River-Norwalk, Inc. Multiple layer fibrous web products of enhanced bulk and method of manufacturing same
US4795668A (en) * 1983-10-11 1989-01-03 Minnesota Mining And Manufacturing Company Bicomponent fibers and webs made therefrom
US4604313A (en) * 1984-04-23 1986-08-05 Kimberly-Clark Corporation Selective layering of superabsorbents in meltblown substrates
US4605702A (en) * 1984-06-27 1986-08-12 American Cyanamid Company Temporary wet strength resin
US4581254A (en) * 1985-03-22 1986-04-08 Union Carbide Corporation Foam applicator used in paper treatment
US4603176A (en) * 1985-06-25 1986-07-29 The Procter & Gamble Company Temporary wet strength resins
US4849054A (en) * 1985-12-04 1989-07-18 James River-Norwalk, Inc. High bulk, embossed fiber sheet material and apparatus and method of manufacturing the same
US4925528A (en) * 1987-04-06 1990-05-15 James River Corporation Of Virginia Manufacture of wetlaid nonwoven webs
US4822452A (en) * 1987-04-06 1989-04-18 James River Corporation Of Virginia Manufacture of wet laid nonwoven webs
US4755421A (en) * 1987-08-07 1988-07-05 James River Corporation Of Virginia Hydroentangled disintegratable fabric
US5019211A (en) * 1987-12-09 1991-05-28 Kimberly-Clark Corporation Tissue webs containing curled temperature-sensitive bicomponent synthetic fibers
US5048589A (en) * 1988-05-18 1991-09-17 Kimberly-Clark Corporation Non-creped hand or wiper towel
US4959125A (en) * 1988-12-05 1990-09-25 The Procter & Gamble Company Soft tissue paper containing noncationic surfactant
US4940513A (en) * 1988-12-05 1990-07-10 The Procter & Gamble Company Process for preparing soft tissue paper treated with noncationic surfactant
JP2682130B2 (en) * 1989-04-25 1997-11-26 三井石油化学工業株式会社 Flexible long-fiber non-woven fabric
US5227107A (en) * 1990-08-07 1993-07-13 Kimberly-Clark Corporation Process and apparatus for forming nonwovens within a forming chamber
US5129988A (en) * 1991-06-21 1992-07-14 Kimberly-Clark Corporation Extended flexible headbox slice with parallel flexible lip extensions and extended internal dividers
US5277976A (en) * 1991-10-07 1994-01-11 Minnesota Mining And Manufacturing Company Oriented profile fibers
US5238534A (en) * 1992-01-24 1993-08-24 James River Corporation Of Virginia Wetlaid nonwovens on high speed machines
US5427696A (en) * 1992-04-09 1995-06-27 The Procter & Gamble Company Biodegradable chemical softening composition useful in fibrous cellulosic materials
US5382400A (en) * 1992-08-21 1995-01-17 Kimberly-Clark Corporation Nonwoven multicomponent polymeric fabric and method for making same
US5336552A (en) * 1992-08-26 1994-08-09 Kimberly-Clark Corporation Nonwoven fabric made with multicomponent polymeric strands including a blend of polyolefin and ethylene alkyl acrylate copolymer
US5240562A (en) * 1992-10-27 1993-08-31 Procter & Gamble Company Paper products containing a chemical softening composition
US5543067A (en) * 1992-10-27 1996-08-06 The Procter & Gamble Company Waterless self-emulsiviable biodegradable chemical softening composition useful in fibrous cellulosic materials
US5494554A (en) * 1993-03-02 1996-02-27 Kimberly-Clark Corporation Method for making soft layered tissues
US5667636A (en) * 1993-03-24 1997-09-16 Kimberly-Clark Worldwide, Inc. Method for making smooth uncreped throughdried sheets
US5399412A (en) * 1993-05-21 1995-03-21 Kimberly-Clark Corporation Uncreped throughdried towels and wipers having high strength and absorbency
US5411636A (en) * 1993-05-21 1995-05-02 Kimberly-Clark Method for increasing the internal bulk of wet-pressed tissue
US5981044A (en) * 1993-06-30 1999-11-09 The Procter & Gamble Company Multi-layered tissue paper web comprising biodegradable chemical softening compositions and binder materials and process for making the same
US5405501A (en) * 1993-06-30 1995-04-11 The Procter & Gamble Company Multi-layered tissue paper web comprising chemical softening compositions and binder materials and process for making the same
US5397435A (en) * 1993-10-22 1995-03-14 Procter & Gamble Company Multi-ply facial tissue paper product comprising chemical softening compositions and binder materials
US5437766A (en) * 1993-10-22 1995-08-01 The Procter & Gamble Company Multi-ply facial tissue paper product comprising biodegradable chemical softening compositions and binder materials
US5385643A (en) * 1994-03-10 1995-01-31 The Procter & Gamble Company Process for applying a thin film containing low levels of a functional-polysiloxane and a nonfunctional-polysiloxane to tissue paper
CA2142805C (en) * 1994-04-12 1999-06-01 Greg Arthur Wendt Method of making soft tissue products
US5558873A (en) * 1994-06-21 1996-09-24 Kimberly-Clark Corporation Soft tissue containing glycerin and quaternary ammonium compounds
US5529665A (en) * 1994-08-08 1996-06-25 Kimberly-Clark Corporation Method for making soft tissue using cationic silicones
US5510000A (en) * 1994-09-20 1996-04-23 The Procter & Gamble Company Paper products containing a vegetable oil based chemical softening composition
US5591309A (en) * 1995-02-06 1997-01-07 Kimberly-Clark Corporation Papermaking machine for making uncreped throughdried tissue sheets
US6203663B1 (en) * 1995-05-05 2001-03-20 Kimberly-Clark Worldwide, Inc. Decorative formation of tissue
US5674590A (en) * 1995-06-07 1997-10-07 Kimberly-Clark Tissue Company High water absorbent double-recreped fibrous webs
US5730839A (en) * 1995-07-21 1998-03-24 Kimberly-Clark Worldwide, Inc. Method of creping tissue webs containing a softener using a closed creping pocket
US5716498A (en) * 1996-04-12 1998-02-10 Witco Corporation Process for softening paper in manufacture
US6211139B1 (en) * 1996-04-26 2001-04-03 Goldschmidt Chemical Corporation Polyester polyquaternary compounds, compositions containing them, and use thereof
US6200669B1 (en) * 1996-11-26 2001-03-13 Kimberly-Clark Worldwide, Inc. Entangled nonwoven fabrics and methods for forming the same
US5935383A (en) * 1996-12-04 1999-08-10 Kimberly-Clark Worldwide, Inc. Method for improved wet strength paper
US6017418A (en) * 1996-12-23 2000-01-25 Fort James Corporation Hydrophilic, humectant, soft, pliable, absorbent paper and method for its manufacture
US6231719B1 (en) * 1996-12-31 2001-05-15 Kimberly-Clark Worldwide, Inc. Uncreped throughdried tissue with controlled coverage additive
US6214146B1 (en) * 1997-04-17 2001-04-10 Kimberly-Clark Worldwide, Inc. Creped wiping product containing binder fibers
US6096152A (en) * 1997-04-30 2000-08-01 Kimberly-Clark Worldwide, Inc. Creped tissue product having a low friction surface and improved wet strength
US5851352A (en) * 1997-05-12 1998-12-22 The Procter & Gamble Company Soft multi-ply tissue paper having a surface deposited strengthening agent
US6248211B1 (en) * 1997-06-16 2001-06-19 Kimberly-Clark Worldwide, Inc. Method for making a throughdried tissue sheet
US6261580B1 (en) * 1997-10-22 2001-07-17 The Procter & Gamble Company Tissue paper with enhanced lotion transfer
US6277241B1 (en) * 1997-11-14 2001-08-21 Kimberly-Clark Worldwide, Inc. Liquid absorbent base web
US6248212B1 (en) * 1997-12-30 2001-06-19 Kimberly-Clark Worldwide, Inc. Through-air-dried post bonded creped fibrous web
US6368609B1 (en) * 1999-04-12 2002-04-09 Kimberly-Clark Worldwide, Inc. Absorbent structure including a thin, calendered airlaid composite and a process for making the composite
US6423180B1 (en) * 1998-12-30 2002-07-23 Kimberly-Clark Worldwide, Inc. Soft and tough paper product with high bulk
US6387495B1 (en) * 1999-04-16 2002-05-14 Kimberly-Clark Worldwide, Inc. Superabsorbent-containing composites
US6241850B1 (en) * 1999-06-16 2001-06-05 The Procter & Gamble Company Soft tissue product exhibiting improved lint resistance and process for making
US20020096281A1 (en) * 1999-11-19 2002-07-25 Hans Wallenius Wet-strong tissue paper
DE60135214D1 (en) * 2000-05-12 2008-09-18 Kimberly Clark Co paper
US6432270B1 (en) * 2001-02-20 2002-08-13 Kimberly-Clark Worldwide, Inc. Soft absorbent tissue
US6752905B2 (en) * 2002-10-08 2004-06-22 Kimberly-Clark Worldwide, Inc. Tissue products having reduced slough
US20040084162A1 (en) * 2002-11-06 2004-05-06 Shannon Thomas Gerard Low slough tissue products and method for making same
US6878238B2 (en) * 2002-12-19 2005-04-12 Kimberly-Clark Worldwide, Inc. Non-woven through air dryer and transfer fabrics for tissue making
US20060144541A1 (en) * 2004-12-30 2006-07-06 Deborah Joy Nickel Softening agent pre-treated fibers

Also Published As

Publication number Publication date
US20030121627A1 (en) 2003-07-03
AU2002349921A1 (en) 2003-06-17
WO2003048453A1 (en) 2003-06-12

Similar Documents

Publication Publication Date Title
TW200300810A (en) Tissue products having reduced lint and slough
EP1558814B1 (en) Multilayered tissue products
US11634870B2 (en) Layered tissue comprising non-wood fibers
TW406154B (en) Soft tissue paper with biased surface properties containing fine particulate fillers
TW318194B (en)
TW440641B (en) Paper products and methods for applying chemical additives to cellulosic fibers
KR100917520B1 (en) Multi-ply tissue product
TW440642B (en) New process for producing creped paper products and creping aid for use therewith
US6911114B2 (en) Tissue with semi-synthetic cationic polymer
CA2280082C (en) Creping adhesive and process for creping tissue paper
TW379273B (en) Process for creeping tissue paper
US6149769A (en) Soft tissue having temporary wet strength
US9518364B2 (en) Wet laid sheet material of a microfibrillated material composition
TW593835B (en) Fibrous materials treated with a polyvinylamine polymer
US20070298221A1 (en) Multi-ply fibrous structures and products employing same
EP3408447B1 (en) Multi-ply fibrous product comprising a laminating adhesive with a dermatologically acceptable acid
JPH11510567A (en) Crepe tissue paper showing unique combination of physical attributes
CZ331197A3 (en) Soft crepe tissue paper
TW200530450A (en) Nonwoven webs having reduced lint and slough
TW201033436A (en) Water-dispersible creping materials
HK1246833A1 (en) Tissue paper comprising pulp fibers originating from miscanthus and method for manufacturing the same
TWI222963B (en) Method of using water-borne epoxies and urethanes in print bonding fluid and products made therefrom
US6336995B1 (en) Cross linked polyamide-ephalohydrin creping additives
US20030111196A1 (en) Tissue products and methods for manufacturing tissue products
AU750550B2 (en) Soft tissue having temporary wet strength