TW200808878A - Coloured superabsorbers - Google Patents
Coloured superabsorbers Download PDFInfo
- Publication number
- TW200808878A TW200808878A TW096113907A TW96113907A TW200808878A TW 200808878 A TW200808878 A TW 200808878A TW 096113907 A TW096113907 A TW 096113907A TW 96113907 A TW96113907 A TW 96113907A TW 200808878 A TW200808878 A TW 200808878A
- Authority
- TW
- Taiwan
- Prior art keywords
- water
- polymer structure
- absorbing polymer
- absorbing
- colorant
- Prior art date
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Classifications
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K3/00—Use of inorganic substances as compounding ingredients
- C08K3/02—Elements
- C08K3/04—Carbon
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- A—HUMAN NECESSITIES
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- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L15/00—Chemical aspects of, or use of materials for, bandages, dressings or absorbent pads
- A61L15/16—Bandages, dressings or absorbent pads for physiological fluids such as urine or blood, e.g. sanitary towels, tampons
- A61L15/42—Use of materials characterised by their function or physical properties
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
- A61L15/00—Chemical aspects of, or use of materials for, bandages, dressings or absorbent pads
- A61L15/16—Bandages, dressings or absorbent pads for physiological fluids such as urine or blood, e.g. sanitary towels, tampons
- A61L15/42—Use of materials characterised by their function or physical properties
- A61L15/60—Liquid-swellable gel-forming materials, e.g. super-absorbents
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F2/00—Processes of polymerisation
- C08F2/44—Polymerisation in the presence of compounding ingredients, e.g. plasticisers, dyestuffs, fillers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08K—Use of inorganic or non-macromolecular organic substances as compounding ingredients
- C08K5/00—Use of organic ingredients
- C08K5/0008—Organic ingredients according to more than one of the "one dot" groups of C08K5/01 - C08K5/59
- C08K5/0041—Optical brightening agents, organic pigments
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F1/00—General methods for the manufacture of artificial filaments or the like
- D01F1/02—Addition of substances to the spinning solution or to the melt
- D01F1/04—Pigments
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F1/00—General methods for the manufacture of artificial filaments or the like
- D01F1/02—Addition of substances to the spinning solution or to the melt
- D01F1/10—Other agents for modifying properties
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- D—TEXTILES; PAPER
- D01—NATURAL OR MAN-MADE THREADS OR FIBRES; SPINNING
- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/02—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D01F6/16—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from homopolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds from polymers of unsaturated carboxylic acids or unsaturated organic esters, e.g. polyacrylic esters, polyvinyl acetate
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- D—TEXTILES; PAPER
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- D01F—CHEMICAL FEATURES IN THE MANUFACTURE OF ARTIFICIAL FILAMENTS, THREADS, FIBRES, BRISTLES OR RIBBONS; APPARATUS SPECIALLY ADAPTED FOR THE MANUFACTURE OF CARBON FILAMENTS
- D01F6/00—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof
- D01F6/28—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D01F6/36—Monocomponent artificial filaments or the like of synthetic polymers; Manufacture thereof from copolymers obtained by reactions only involving carbon-to-carbon unsaturated bonds comprising unsaturated carboxylic acids or unsaturated organic esters as the major constituent
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61F—FILTERS IMPLANTABLE INTO BLOOD VESSELS; PROSTHESES; DEVICES PROVIDING PATENCY TO, OR PREVENTING COLLAPSING OF, TUBULAR STRUCTURES OF THE BODY, e.g. STENTS; ORTHOPAEDIC, NURSING OR CONTRACEPTIVE DEVICES; FOMENTATION; TREATMENT OR PROTECTION OF EYES OR EARS; BANDAGES, DRESSINGS OR ABSORBENT PADS; FIRST-AID KITS
- A61F13/00—Bandages or dressings; Absorbent pads
- A61F13/15—Absorbent pads, e.g. sanitary towels, swabs or tampons for external or internal application to the body; Supporting or fastening means therefor; Tampon applicators
- A61F13/53—Absorbent pads, e.g. sanitary towels, swabs or tampons for external or internal application to the body; Supporting or fastening means therefor; Tampon applicators characterised by the absorbing medium
- A61F2013/530481—Absorbent pads, e.g. sanitary towels, swabs or tampons for external or internal application to the body; Supporting or fastening means therefor; Tampon applicators characterised by the absorbing medium having superabsorbent materials, i.e. highly absorbent polymer gel materials
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Textile Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Polymers & Plastics (AREA)
- Medicinal Chemistry (AREA)
- Veterinary Medicine (AREA)
- Epidemiology (AREA)
- Manufacturing & Machinery (AREA)
- General Health & Medical Sciences (AREA)
- Animal Behavior & Ethology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hematology (AREA)
- Public Health (AREA)
- Materials Engineering (AREA)
- Dispersion Chemistry (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Absorbent Articles And Supports Therefor (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Abstract
Description
200808878 九、發明說明: 【發明所屬之技術領域】 本發明係關於吸水性聚合物結構、用來製造吸水性聚 合物結構的方法、可利用此方法獲得之吸水性聚合物結 構、包含吸水性聚合物結構及基材的複合物、用來製造複 合物之方法、可利用此方法獲得的複合物、包含吸水性聚 合物結構或複合物的化學產物以及吸水性聚合物結構或複 合物在化學產物中之用途。 【先前技術】 起吸收劑為一種水不溶的交聯聚合物,其能藉由膨脹 及形成水凝膠而吸收大量水性液體,特別是體液,較佳為 尿或血液,且在既定壓力下保留之。因為這些特徵性質, 些聚合物主要透過摻入衞生用品,諸如例如嬰兒尿布、 失禁產品或女性衞生用品中提供應用。 起及收劑之製造通常猎由攜帶酸基團之單體在交聯劍 存在下之自由基聚合反應而進行。在此方法中,藉由選擇 單體組成物、交聯劑和聚合條件及在聚合後所獲得水凝膠 的方法條件,可製造出具有不同吸收性質之聚合物。進一 步可月b性係藉由製造接枝聚合物而提供,例如藉由根據 DE-OS 26 12 846使用經化學改質的澱粉類、纖維素類及 聚乙烯醇’以及例如根據DE 40 20 780 C1後交聯聚合物 顆粒的表面來後處理水凝膠或在乾燥水凝膠之後所獲得的 粉末狀聚合物顆粒。藉由吸水性聚合物顆粒表面的後交 聯’特別是聚合物顆粒在壓力效應下之吸收容量會增加。 200808878 為了美觀及因為環请德ft ΛΑ τα» 1衣現規點的理由,設計更小且更薄的 衛生用品有漸增之趨勢。為了達成衛生用品的固定總保留 容量’此需求僅可藉由減少龐大毛絮之比例來滿足。因此, 吸水性聚合物漸漸形成衛生用品的主要組分。 ^從先前技術,例如從DE 40 20 780 C1得知的超吸收 劑通常為白色。但是’這有在較佳與相·對應著色的内衣組 口使用的著色衞生用品中,白色超吸收劑顆粒會不利地影 響著色衛生用品之外觀的缺點,尤其是若大量使用超吸收 劑顆粒時。 除了白色超吸收劑顆粒會不適宜地影響著色衛生用品 外觀之缺點外,在此技藝中已知之超吸收劑經常無法充分 有效地黏結在體液中令人不愉快的臭味化合物。為此理 由,US 2〇〇4/〇12681建議對包含在吸收物件中的基材表面 之塗知I合材料及活化試劑,然後加熱至在1 〇〇。(3至3 00 c之間的溫度,藉此聚合材料藉由活化試劑及加熱而轉換 _ 成活性碳。以此方式形成的活性碳能吸附令人不愉快的臭 味化合物。但是,此方法對臭味控制的缺點在於例如對溫 度增加敏感之基材表面無法以此方式用活性碳塗佈。進一 步缺點在於在尿布作為吸收物件的情況中,活性碳塗層至 夕4为會因尿布穿戴者之移動而磨擦掉,使其出現在尿布 外。 【發明内容】 因此’本發明具有克服由先前技術引起的缺點之目標。 本發明特別具有提供超吸收劑或包含超吸收劑之複合 200808878 物的目標,尤其是它們的特徵為其 品中而沒有美觀上的缺點。 亦可使用在著色衛生 用 根據本發明之進 7规點,兀說由 、, 不僅應該提供可使用在著 色衛生用品中而沒有美觀上缺點夕_ > 、 點之超吸收劑或包含超吸收 劑的複合物,而且這些超吸收劑或 ^ 些獲合物亦各別應該 在特別的具體實例中亦能夠儘可能右#仏★ j此有效地黏結令人不愉快 的臭味化合物,該臭味化合物特別白 符別包含在體液中或其會透200808878 IX. OBJECTS OF THE INVENTION: TECHNICAL FIELD The present invention relates to a water-absorbing polymer structure, a method for producing a water-absorbing polymer structure, a water-absorbent polymer structure obtainable by the method, and a water-absorbent polymerization. a composite of a structure and a substrate, a method for producing a composite, a composite obtainable by the method, a chemical product comprising a water-absorbing polymer structure or a composite, and a water-absorbing polymer structure or composite in a chemical product Use in the middle. [Prior Art] The absorbent is a water-insoluble cross-linked polymer capable of absorbing a large amount of an aqueous liquid, particularly a body fluid, preferably urine or blood, by swelling and forming a hydrogel, and retaining under a predetermined pressure. It. Because of these characteristic properties, some polymers are primarily provided for use by incorporation into hygiene articles such as, for example, baby diapers, incontinence products, or feminine hygiene products. The manufacture of the collector and the collector is usually carried out by radical polymerization of a monomer carrying an acid group in the presence of a crosslinked sword. In this method, polymers having different absorption properties can be produced by selecting the monomer composition, the crosslinking agent, and the polymerization conditions and the process conditions of the hydrogel obtained after the polymerization. Further, the monthly b-type is provided by the production of a graft polymer, for example by the use of chemically modified starches, celluloses and polyvinyl alcohols according to DE-OS 26 12 846 and, for example, according to DE 40 20 780 The surface of the polymer particles is crosslinked after C1 to post-treat the hydrogel or the powdery polymer particles obtained after drying the hydrogel. The post-crosslinking by the surface of the water-absorbing polymer particles, particularly the polymer particles, increases in the absorption capacity under the pressure effect. 200808878 In order to be aesthetically pleasing and because of the reasons for the ring, the design of smaller and thinner sanitary products is on the rise. In order to achieve a fixed total reserve capacity of sanitary products, this demand can only be met by reducing the proportion of large batt. Therefore, the water-absorbing polymer gradually forms a main component of the sanitary article. The superabsorbent known from the prior art, for example from DE 40 20 780 C1, is usually white. However, 'this has the disadvantages of white superabsorbent particles which adversely affect the appearance of colored sanitary articles in colored sanitary articles which are preferably used in the corresponding color-matched undergarment group, especially if a large amount of superabsorbent particles are used. . In addition to the disadvantages of white superabsorbent particles which undesirably affect the appearance of colored sanitary articles, superabsorbents known in the art are often not sufficiently effective to adhere to unpleasant odor compounds in body fluids. For this reason, US 2 〇〇 4/〇 12681 suggests coating the surface of the substrate contained in the absorbent article with the active material and the activating reagent, and then heating to 1 Torr. (a temperature between 3 and 300 00 c, whereby the polymeric material is converted to activated carbon by an activating reagent and heating. The activated carbon formed in this manner can adsorb an unpleasant odorous compound. However, this method is A disadvantage of odor control is that, for example, the surface of the substrate sensitive to temperature increase cannot be coated with activated carbon in this way. A further disadvantage is that in the case of a diaper as an absorbent member, the activated carbon coating is due to the diaper wearer. The invention is rubbed off to cause it to appear outside the diaper. [Invention] The present invention has the object of overcoming the disadvantages caused by the prior art. The present invention particularly has a superabsorbent or a composite 200808878 comprising a superabsorbent. The objects, especially their characteristics, are in their products without aesthetic disadvantages. They can also be used in coloring hygiene according to the invention, and should not only be provided for use in colored hygiene products. There is no aesthetic disadvantage _ > , superabsorbent or superabsorbent-containing composite, and these superabsorbents or some of the extracts are also Should not be as special as possible in the specific example. #仏★ j This effectively binds an unpleasant odor compound, which is especially white in the body fluid or it will be transparent.
過細菌分解包含在體液中的化合物而產生。 儘管有上述描述的優點,這些超吸收劑或各別包含超 吸收劑之複合物應該具有好的皮膚耐受性及其它優良的吸 收性質。 在本發明下的進-步目標為提供可製備具有上述優點 之超吸收劑和包含超吸收劑的複合物之方法。 對工地目標之解決方法之貢獻係藉由吸水性、較佳經 者色的聚合物結構達成,以吸水性聚合物結構的總重量為 準’該聚合物結構包括〇 〇〇1至1〇重量%,特別佳為〇 〇1 :5重量%及最佳為〇1至2重量%之著色劑,藉此吸水性 κ 0物…構的特徵為根據於本文描述的測試方法所測定之 根據L,a,b色彩系統之L值少於90,較佳少於8〇,而更佳 為少於70,❿更佳為少於60及最佳少於50。 對上述目標之解決方法之貢獻亦藉由吸水性、較佳經 著色的來5物結構達成,以吸水性聚合物結構的總重量為 準,該來合物結構包括〇·〇〇1至10重量。/〇,特別佳為〇·〇ΐ 至5重1%及最佳為0·ι至2重量%之著色劑,其中該著色 8 200808878 劑均勻地分佈在吸水性結構内部。 著色劑”均勻分佈,,在吸水性聚合物結構内部於此經了 解特別為特徵如下之分佈:在具有最高著色劑濃度的吸水 性聚合物結構區域中之著色劑濃度為在具有最低著色劑濃 度的吸水性聚合物結構區域中之著色劑濃度的至多倍 大,特別佳為至多5倍大及最佳為至多2倍大。Produced by bacteria that decompose compounds contained in body fluids. Despite the advantages described above, these superabsorbents or composites each comprising a superabsorbent should have good skin tolerance and other excellent absorbent properties. A further object underlying the present invention is to provide a process for preparing a superabsorbent having the above advantages and a composite comprising a superabsorbent. The contribution to the solution to the site objectives is achieved by a water-absorbent, better-performing polymer structure based on the total weight of the water-absorbing polymer structure. The polymer structure comprises 〇〇〇1 to 1 〇 weight. %, particularly preferably 〇〇1:5 wt% and preferably 〇1 to 2 wt% of a coloring agent, whereby the characteristic of the water absorbing material is determined according to the test method described herein according to L The a, b color system has an L value of less than 90, preferably less than 8 inches, more preferably less than 70, more preferably less than 60 and most preferably less than 50. The contribution to the solution to the above objectives is also achieved by the water-absorbing, preferably colored, structure of the material, based on the total weight of the water-absorbing polymer structure, which comprises 〇·〇〇1 to 10 weight. / 〇, particularly preferably 〇·〇ΐ to 5 weight 1% and preferably 0. ι to 2% by weight of the coloring agent, wherein the coloring 8 200808878 agent is evenly distributed inside the water absorbent structure. The colorant is uniformly distributed, and it is hereby known within the structure of the water-absorbing polymer that it is characterized by a distribution in which the concentration of the colorant in the region of the water-absorbing polymer structure having the highest colorant concentration is at the lowest colorant concentration. The concentration of the colorant in the water-absorbing polymer structure region is at most times larger, particularly preferably at most 5 times large and most preferably at most 2 times larger.
^ L,a,b色彩系統為在1976年由CIE委員會&CIE_XYZ_ 模型發展出的色彩“。其係標準化、等間隔且裝置無關。 根據本發明的吸水性聚合物結構之特別具體實例,這 些的特徵為根據於本文描述的贼方法所測量之根據 色^系統之&值的量大於1,較佳大於4,特別佳大於1〇 最4土大於2G ’以及根據L,a,b色彩系統之b值的量大於 8,較佳大於15,特別佳大於3〇及最佳大於4〇。 根據本發明較佳的聚合物結構有纖維、泡㈣或顆粒, 其中緘維及顆粒較佳且顆粒特別佳。 根據本發明的較佳聚合物纖維按規格尺寸切割,们 它們可摻人或作為纺織品用之紗線且亦可直接掺入纺織』 I根據本發明較佳的是,聚合物纖維具有範圍從工至 先米車又仏為2至500毫米及特別佳為5至1〇〇毫米的^ 度;及範圍從…00丹尼爾(Denier),較佳為3至1〇 丹尼爾及特別佳為5至60丹尼爾的直徑。 根據本發明的較佳聚合物顆粒按規格尺寸切割,使$ 它們具有範圍從H)至蓮微米,較佳為2〇至聰微; 及考寸則土為150至85〇微米之根據ERT 之平均身 9 200808878 米尺寸。然後特別佳的是,具有範圍從300至600微米之 顆粒尺 心來合物顆粒部分為至少25重量%,特別佳為至 5 0 -母..0/ 77 〇 里里/。及最佳為至少75重量%,以吸水性聚合物顆 粒的總重量為準。 在根據本發明的吸水性聚合物結構之較佳具體實例 =二為經表面後交聯者。透過後交聯,聚合物結構的 1部區域之交聯程度比内部區域高,以便形成一核殼杜 才冓。 再者,根據本發明較佳的是吸水性聚合物結構以下列 為基礎: (α1) 2〇’.998重量%,較佳為55_98·99重量%及特 其佳為70至98_79重量%之經聚合的乙烯屬不飽和攜帶酸 二團之早體或其鹽類或包含質子化或四級化氮之經聚合乙 ::不飽和單體或其混合物,其中至少包含乙烯屬不飽和 s酉夂基團單體、較佳肖合$ μ 早1匕θ兩烯酸之混合物特別佳; (α2) 〇_80重量%,翁、杜劣 λ 0〗^ 季又^土為〇-牧99重量%及特別佳為 4-44.89重量%可與(αΐ)此取 單體· /、♦ 5之經聚合單乙烯屬不飽和 U3) 0.001-5重量%,糖杜劣λ 〇 仓為〇.01*3重量%及特別佳為 0.01-2.5重量%之一或多種交聯劑; 巧 (α4) 0.001-10 重量%〆 ^ 軏佳為〇·〇1-5重量%及最佳為 ϋ· 1 -2重置%的者色劑; (α5) 0-30重量%,較伟失 舌曰 為〇-5重量%及特別佳為0.1-5 重2: %之水溶性聚合物; 10 200808878 Λ/ U6) 0-20重量%,較佳為2 5_15重量%及特別佳為% io重量%的水;和 (α7) 0-20重量%,較佳為〇·1〇重量%及特別佳為 8重量〇/〇之一或多種添加劑; 其中〇1)至(α7)重量總和為1⑽重量0/〇。 單乙烯屬不飽和含酸基團單體(α1)可部分或完全,較 4係硭刀、、二中和。單乙浠屬不飽和含酸基團單體經中和到 _ 至少25莫耳%較佳,到至少50莫耳%特別佳而到5〇_8〇莫 耳%更佳。在此上下文中,參考DE 19$ 29 348 αι,此揭 不在此納入作為參考。中和亦可在聚合之後部分或完全地 進行再者,中和可以驗金屬氫氧化物、驗土金屬氫氧化 =、氨和碳酸鹽及碳酸氫鹽進行。此外,任何與酸形成水 /合性鹽之進一步鹼為可想見者。以不同鹼來混合中和亦為 可想見者。以氨及驗金屬氫氧化物中和較佳,以氯氧化納 及以氨特別佳。 • 再者在聚合物結構中,自由酸基團可佔絕大多數,以 便此來合物結構具有位於酸範圍# pH值。此酸性吸水性 聚合物結構可至少部分由與酸性聚合物比較呈驗性之包含 自由鹼基團(較佳為胺基團)之聚合物中和。這些聚合物在 文獻中%為”混合床離子交換吸收聚合物”聚合 物),尤其是揭示在W0 99/34843中。w〇 99/34843之揭示 於此以參考方式納入,因此為本揭示的部分。料來說, 二EA聚合物代表一種一方面包含能夠交換陰離子之鹼性 爻白物及另方面包含與鹼性聚合物比較呈酸性且能夠交 11 200808878 換陽離子的聚合物之組成物。鹼性聚合物包含鹼基團且典 型係藉由攜帶鹼基團或可轉換成鹼基團的基團之單體的聚 合反應獲得。這些單體特別有包含一級、二級或三級胺類 或相對應膦類或至少二種前述提及的官能基者。此單體群 組特別包括伸乙基胺、烯丙胺、二烯丙胺、4_胺基丁、烯、 烧氧基環烯(alkyl〇XyCyClene)、乙烯基甲醯胺、5_胺基戊烯、 碳二醯亞胺、甲醛達胺(formaldacin)、黑色素及其類似物、 和其二級或三級胺衍生物。 作為乙烯屬不飽和含酸基團單體(α1),使用在 2004/037903(其藉此納入作為參考,因此形成本揭示的部 分)中提到為乙烯屬不飽和含酸基團單體的化合物較 佳。特別佳的乙烯屬不飽和含酸基團單體(α1)有丙烯酸及 曱基丙烯酸,其中丙烯酸最佳。 根據本發明的聚合物結構之具體實例,可與(αΐ)共聚 合的單乙烯屬不飽和單體(α2)有丙烯醯胺類、甲基丙烯醯 胺類或乙烯醯胺類。 除了丙烯醯胺及甲基丙烯醯胺之外,較佳的(甲基)丙 烯酿胺類有經烷基取代的(甲基)丙烯醯胺類或(甲基)丙烯 Si胺類之經胺烷基取代的衍生物,諸如Ν_羥曱基(甲基)丙 烯酿胺、Ν,Ν-二曱基胺基(甲基)丙烯醯胺、二曱基(甲基) 丙烯醯胺或二乙基(甲基)丙烯醯胺。可能的乙烯醯胺類有 例如Ν-乙烯醯胺類、Ν-乙烯甲醯胺類、Ν-乙烯乙醯胺類、 Ν-乙烯基_Ν-曱基乙醯胺類、Ν_乙烯基_Ν-甲基曱醯胺類、 乙烯吡咯啶酮。在這些單體當中,丙烯醯胺特別佳。 12 200808878 根據本發明的聚合物姓 1) 共聚合的單乙烯屬不钓^之另—個具體實例,可與u 上下文中,特別是&气A 體“2)為水溶性單體。在此 ^疋坑乳基-聚氧化烯(曱臬彳而、瞭醅萨類如甲 氧基-聚乙二醇(甲其p A 基)丙烯酸酉曰類如甲 甲基)丙烯酸s旨類較佳。^ The L, a, b color system is a color developed by the CIE Committee & CIE_XYZ_ model in 1976. It is standardized, equally spaced and device-independent. According to a particular embodiment of the water-absorbing polymer structure of the present invention, these Characterized according to the thief method described herein, the amount of & value according to the color system is greater than 1, preferably greater than 4, particularly preferably greater than 1 〇 most 4 soil greater than 2G 'and according to L, a, b color The b value of the system is greater than 8, preferably greater than 15, particularly preferably greater than 3 Torr and most preferably greater than 4 Torr. Preferred polymeric structures in accordance with the present invention are fibers, blister (4) or granules, wherein bismuth and granules are preferred. The granules are particularly preferred. The preferred polymeric fibers according to the present invention are cut to size, they may be blended or used as yarns for textiles and may be incorporated directly into the woven fabric. I. Preferred according to the invention, polymerization The fiber has a range of from 2 to 500 mm and particularly preferably from 5 to 1 mm, and ranges from ...00 Denier, preferably 3 to 1 denier and Particularly preferably a diameter of 5 to 60 denier. The preferred polymer particles of the invention are cut to size such that they have a range from H) to lotus micron, preferably 2 to Congwei; and the test is soiled to 150 to 85 microns. 9 200808878 Meter size. It is then particularly preferred that the portion of the granules having a particle size ranging from 300 to 600 microns is at least 25% by weight, particularly preferably up to 50-mother..0/77 〇里里/ And preferably at least 75% by weight, based on the total weight of the water-absorbing polymer particles. A preferred embodiment of the water-absorbing polymer structure according to the present invention = two is a post-crosslinker. Further, the cross-linking degree of one region of the polymer structure is higher than that of the inner region to form a core shell. In addition, according to the present invention, the water-absorbent polymer structure is based on the following: (α1) 2〇'.998% by weight, preferably 55-98.99% by weight and particularly preferably 70 to 98-79% by weight of the polymerized ethylenically unsaturated acid-bearing dimers or their salts or containing protonated or Polymerization of quaternary nitrogen: B: unsaturated monomers or mixtures thereof, It is particularly preferable to contain at least a monomer of an ethylenically unsaturated sulfonium group, preferably a mixture of $μ1 and 匕2 octadioic acid; (α2) 〇80% by weight, Weng, Du λ 0〗 The season is also 99% by weight of 〇-牧牧, and particularly preferably 4-44.89% by weight, and (αΐ) is obtained by polymerizing monoethylenically unsaturated U3) 0.001-5% by weight. Sugar 杜 λ Kamakura is 〇.01*3 wt% and particularly preferably 0.01-2.5 wt% one or more cross-linking agents; Qiao (α4) 0.001-10 wt% 〆^ 軏佳为〇·〇1- 5 wt% and most preferably ϋ·1 -2 reset % of the toner; (α5) 0-30 wt%, 伟 失 失 曰 〇 重量 重量 重量 重量 及 及 及 及 及 及 及 及 及 及 及 及 及 及 及 及 及 及% water-soluble polymer; 10 200808878 Λ / U6) 0-20% by weight, preferably 2 5 - 15% by weight and particularly preferably % io% by weight of water; and (α7) 0-20% by weight, preferably 〇·1〇% by weight and particularly preferably one or more additives of 8 parts by weight/〇; wherein the total weight of 〇1) to (α7) is 1 (10) by weight 0/〇. The monoethylenically unsaturated acid group-containing monomer (α1) may be partially or completely, compared with the 4-system file, and the second neutralization. The monoethylidene unsaturated acid group-containing monomer is preferably neutralized to at least 25 mol%, more preferably at least 50 mol%, and more preferably 5 〇 8 〇 mol%. In this context, reference is made to DE 19$ 29 348 α, which is incorporated herein by reference. Neutralization may also be carried out partially or completely after the polymerization, and the neutralization may be carried out by measuring metal hydroxide, soil metal hydroxide =, ammonia and carbonate, and hydrogencarbonate. In addition, any further base which forms a water/combination salt with an acid is conceivable. It is also conceivable to mix and neutralize with different bases. It is preferred to neutralize the ammonia and the metal hydroxide, and it is particularly preferable to oxidize chlorine with ammonia. • Again, in the polymer structure, free acid groups can be dominant, so that the structure of the complex has a pH range of pH #. The acidic water-absorbing polymer structure can be at least partially neutralized by a polymer comprising a free base group (preferably an amine group) which is comparable to an acidic polymer. These polymers are in the literature "% mixed bed ion exchange absorbing polymer" polymers, especially disclosed in WO 99/34843. The disclosure of WO 〇 99/34,843 is hereby incorporated by reference, and is hereby incorporated by reference. In the meantime, the di-EA polymer represents a composition comprising a basic ruthenium capable of exchanging anions on the one hand and a polymer which is acidic compared to a basic polymer and capable of undergoing cation exchange. The basic polymer contains a base group and is typically obtained by a polymerization reaction of a monomer carrying a base group or a group convertible into a base group. These monomers are particularly those which comprise a primary, secondary or tertiary amine or a corresponding phosphine or at least two of the aforementioned functional groups. This monomer group includes, in particular, ethylamine, allylamine, diallylamine, 4-aminobutyl, alkene, alkylox XyCyClene, vinylformamide, 5-aminopentene , carbodiimide, formaldacin, melanin and its analogs, and its secondary or tertiary amine derivatives. As the ethylenically unsaturated acid group-containing monomer (α1), the use of the ethylenically unsaturated acid group-containing monomer is referred to in 2004/037903, which is incorporated herein by reference in its entirety in its entirety. The compound is preferred. Particularly preferred ethylenically unsaturated acid group-containing monomers (?1) are acrylic acid and mercaptoacrylic acid, of which acrylic acid is most preferred. According to a specific example of the polymer structure of the present invention, the monoethylenically unsaturated monomer (?2) copolymerizable with (??) may be acrylamide, methacrylamide or vinylamine. In addition to acrylamide and methacrylamide, preferred (meth)acrylamides are alkyl-substituted (meth) acrylamide or (meth) propylene Si amine amines. Alkyl-substituted derivatives such as hydrazine-hydroxyindole (meth) acrylamide, hydrazine, hydrazine-didecylamino (meth) acrylamide, dimercapto (meth) acrylamide or two Ethyl (meth) acrylamide. Possible vinyl amides are, for example, hydrazine-vinyl decylamine, hydrazine-ethylene carbamide, hydrazine-ethylene acetamide, hydrazine-vinyl hydrazine-mercaptoacetamide, Ν_vinyl _ Ν-methyl decylamine, vinyl pyrrolidone. Among these monomers, acrylamide is particularly preferred. 12 200808878 The polymer 1 according to the invention is a water-soluble monomer in the context of the copolymerization of monovinyl genus, which may be in the context of u, in particular & gas A "2".疋 疋 乳 - - 聚 聚 聚 - - - - 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳 乳good.
2) ,可分分與Ul)共聚合的單乙烯屬不飽和單體U 丙稀酸單財讀°料可分散在水巾的單體, r (甲^、甲基丙烯酸酿類較佳,諸如(曱基)丙烯酸甲 丁此 lT&)丙烯酸丙酯或(甲基)丙烯酸 J Θ曰0 可與㈣共聚合之單乙烯屬不飽和單體(⑼進一步包 括甲基聚乙二醇烯丙基醚類、醋酸乙稀酯、苯 異丁 烯。 乍為又耳外诏(α3),使用在WO-A-20〇4/〇37903中提到 乍為又%p ^ ( aj)的化合物較佳。在這些交聯劑當中,水溶 性:聯劑特別佳。最佳A N,N,·亞甲基雙丙烯醯胺、聚乙 二醇二(甲基)丙烯酸酯類、氯化三烯丙基甲基銨、氯化四 烯丙基銨和每莫耳丙烯酸與9莫耳環氧乙烷製備之丙烯酸 烯丙基九乙二醇酯。 作為著色劑(a4),可在根據本發明之聚合物結構中包 含無機及有機著色劑二者,其中這些著色劑可為水溶性或 水不溶性。 在根據本發明的聚合物結構之較佳具體實例中,這些 包括無機或有機、較佳粉末狀顏料作為著色劑。顏料與染 料之差異在於它們在應用媒質中的不溶程度。 13 200808878 顏料通常根據色彩索引(C.L)來分類,其中除了系統名 稱或俗名之外,尚加入能夠清楚分類的C I.描述。 合適的無機顏料及製造方法可在下列文獻中找到:G 巴西鮑(Buxbaum)的,,工業無機顏料,,,第i版,第85_ι〇7 頁,VCH Verlagsgesellschaft mbH,魏因海姆(weinheim), B93; G.巴西鮑的”工業無機顏料”,第】版,第ιΐ4_ιΐ7 頁,VCH Verlagsgesellschaft mbH,魏因海姆,1993 ;及 G.巴西鮑的,,工業無機顏料,,,第i版’第i24_i3i頁,vch Verlagsgesellschaft mbH,魏因海姆,! 993。這些文件關於 無機顏料的揭示藉此納人作為參考且形成本發明之揭示的 部分。 作為較佳的無機顏料,提到的有具有綠色或藍色顏色 之銅酞花青顏料。、綠色顏色通常藉由以氯原子取代在大環 四胺處的氫而造成。更合適的無機顏料有I紫色顏料(式 MnNH4P2〇7的焦填酸鹽或氨與龜(ΙΠ),纟藉由化學計量組 成的變化來提供較藍或較紅之色調)、群青顏料(鈉矽酸鹽、 銘石夕酸鹽)、以例如具有尖晶石結構的鉻氧化物或純化物 為主之藍色及綠色顏料。此些顏料可以下列商品名稱商業 購得:Heiiogen⑨-藍色、Heli〇gen@_綠色、仏—⑽·綠色、2), can be divided into Ul) copolymerized monoethylenically unsaturated monomer U acrylic acid single reading material can be dispersed in the water towel monomer, r (methyl, methacrylic brewing is better, Such as (mercapto) methacrylate, this lT&) propyl acrylate or (meth)acrylic acid J Θ曰0 can be copolymerized with (tetra) a monoethylenically unsaturated monomer ((9) further includes methylpolyethylene glycol allylate An ether, a vinyl acetate, a phenylisobutylene. The oxime is an external sputum (α3), and a compound in which 乍 is %p ^ ( aj) is preferably used in WO-A-20〇4/〇37903. Among these cross-linking agents, water-soluble: the crosslinking agent is particularly preferred. The best AN, N, · methylene bis acrylamide, polyethylene glycol di (meth) acrylate, triallyl chloride Methylammonium, tetraallyl ammonium chloride and allyl nonaethylene glycol acrylate prepared per mole of acrylic acid with 9 moles of ethylene oxide. As colorant (a4), a polymer according to the invention Both inorganic and organic colorants are included in the structure, wherein the colorants may be water soluble or water insoluble. Preferred in the polymer structure according to the present invention. In specific examples, these include inorganic or organic, preferably powdered pigments as colorants. Pigments differ from dyes in their degree of insolubility in the applied medium. 13 200808878 Pigments are usually classified according to color index (CL), except for systems. In addition to the name or the common name, a description of the C I. can be clearly classified. Suitable inorganic pigments and methods of manufacture can be found in the following literature: G, Buxbaum, Industrial Inorganic Pigments,, i, Page 85_ι〇7, VCH Verlagsgesellschaft mbH, Weinheim, B93; G. Brazil's “Industrial Inorganic Pigments”, ed., pp. 4_ιΐ7, VCH Verlagsgesellschaft mbH, Weinheim, 1993; and G. Brazil Abalone, Industrial Inorganic Pigments,, i.S. pp. i24_i3i, vch Verlagsgesellschaft mbH, Weinheim, 993. These documents are hereby incorporated by reference in their entirety for all of the disclosure of the disclosure. As preferred inorganic pigments, there are mentioned copper phthalocyanine pigments having a green or blue color. Green color Often caused by the substitution of a chlorine atom for the hydrogen at the macrocyclic tetraamine. A more suitable inorganic pigment is a violet pigment (a pyroantate of the formula MnNH4P2〇7 or ammonia and a turtle (ΙΠ), by stoichiometry a change in composition to provide a bluer or redder shade), a cyanine pigment (sodium citrate, a sulphate), a blue or green color based on, for example, a chromium oxide or a purified substance having a spinel structure Pigments. These pigments are commercially available under the following trade names: Heiiogen 9-blue, Heli〇gen@_green, 仏-(10)·green,
SiC〇P_-藍色(BASF AG的註冊商標)和群青、鉻氧化 物或錳紫色顏料。進一步較佳作為無機顏料的有茜素茜草 沉澱色料 '鋇黃、鉻黃、絡綠、氧化鉻綠、絡橙、絡紅、 天藍料(centum)、氧化鐵黃、曰光·堅牢黃、heH〇gen誌、 、綠、印度黃、姑藍、姑黃、銘綠、始紫、鐘該、 200808878 !Γ錄:黃、持久綠、持久紅、Schweinf•綠、銷黃、群 月▲、群月紫、水綠礬、動物黑、氧化鐵黑、象牙里、鮮 黑、錳黑、植物黑或石板瓦黑。 …燈 根據C.I·第1部,進一步較^ /平乂 1土的無機顏料有 28、 顏料藍色29、顏料g色36、多g αι ^ ^^色 颂村孤邑36、顏料棕色24、 29、 顏料棕色31、顏料 色 _ , 顏料紅色101、顏料龙念 42、顏料黃色53、顏料黃色 色 色!5。 顏抖!色184、顏料紫 參 ^上述提及的無機顏料通常具有平均顆粒直徑〇 200 Μ米,較佳從〇丨 至 上立η 微未’特別佳從〇·25至50婵 米及隶佳從〇·75至7·5微米。 至50喊 在無機顏料當中,特別佳的 %,特別佳至少95重量%及曰/、機顏科為至少90重量 機顏料的總重量為準)以碳;^至少"重量%(各別以無 中,碳、煤灰m / 者。在這些無機顏料當 因為二二=及碳特別佳,其中活性碳最佳, 會黏結討厭的臭味。,,、、,:物顆粒,而且其_ 非曰#^^ 碳,,經了解為最小的石墨結晶及 非日日形奴且具有多孔結構 平方公尺/克間之碳結構。錢面積較佳在綱至测 合適的有機顏料及製造 m η 乃在可特別採自W.赫伯斯特SiC〇P_-blue (registered trademark of BASF AG) and ultramarine blue, chromium oxide or manganese violet pigment. Further preferred as an inorganic pigment, the alfalfa valerian sediment coloring material 'yellow yellow, chrome yellow, complex green, chrome oxide green, orange, red, skyum, iron oxide yellow, twilight, fast yellow, heH〇gen Zhi, Green, Indian Yellow, Gu Lan, Gu Huang, Ming Green, Shi Zi, Zhong Zhi, 200808878 ! Record: Yellow, Persistent Green, Long Lasting Red, Schweinf•Green, Pin Yellow, Group Moon ▲, Groups of purple, water green, animal black, iron oxide black, ivory, fresh black, manganese black, plant black or slate black. ...light according to CI·Part 1, further than the inorganic pigment of ^ / 乂 1 soil 28, pigment blue 29, pigment g color 36, more g αι ^ ^^ 颂 颂 邑 邑 、 36, pigment brown 24, 29, pigment brown 31, pigment color _, pigment red 101, pigment dragon read 42, pigment yellow 53, pigment yellow color! 5. Yan shake! Color 184, pigment purple ginseng ^ The above-mentioned inorganic pigment usually has an average particle diameter of Μ200 Μm, preferably from 〇丨 to the upper η micro-not particularly good from 〇·25 to 50 婵米 and Lijia from 〇· 75 to 7. 5 microns. To 50% of the inorganic pigments, particularly good %, especially preferably at least 95% by weight and 曰 /, machine section is the total weight of at least 90 weight machine pigments) to carbon; ^ at least "% by weight (each Nothing, carbon, coal ash m /. In these inorganic pigments because of the second and second = and carbon is particularly good, of which the best activated carbon, will stick to the nasty odor.,,,,: particles, and its _ non-曰#^^ carbon, known as the smallest graphite crystal and non-Japanese-style slaves with a porous structure of square meters / gram of carbon structure. The money area is better to the appropriate organic pigments and manufacturing m η is especially available from W. Herbst
(Herbst)及 Κ·漢爵(H ,第 2 版,第 4_u 百的—一·•一★ mbH^S^^,1995;w 5 VCH Verlagsgesellschaft 〇rganische Pigmente^ , ^ ^ ^ ^ ^ ^Industrielle(Herbst) and Κ··············································^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^^
昂2版,第462頁,VCH 15 200808878Ang 2, page 462, VCH 15 200808878
Verlagsgesellschaft mbH,魏因海姆,、995 ; W.赫伯斯特 反 Κ·漢爵的 ”Industrielle organische Pigmente”,第 2 版, 第 482-485 頁,VCH Verlagsgesellschaft mbH,魏因海姆, 1995 ; W·赫伯斯特及 K·漢爵的 Ρζ·公,第 2 版,第 503 頁,VCH Verlagsgesellschaft mbH.,,巍因海姆,l"5 ;和 W·赫伯斯特及Κ·漢爵 的’’Industrielle organische Pigmente,,,箄 2 版,第 567-569 頁,VCH Verlagsgesellschaft mbH,魏因海姆,1995。 特別佳的有機顏料有偶氮顏料如單偶氮顏料、重氮顏 料、β-萘酚顏料、萘酚-AS-顏料、塗漆偶氮顏料、苯并咪 唑烷(benzimidazolan)顏料、重氮縮合顏料、偶氮_金屬錯 合物及異吲哚啉酮顏料及異吲哚啉顏料。作為合適的多環 顏料,提到的有酞花青顏料、硫靛顏料及特別佳的瓷吖啶 酮(chinaeridon)顏料及茈顏料和茜酮(perin〇n)顏料。更合 適的多環有機顏料有蒽醌顏料如蒽嘧啶顏料、黃烷士酮顏 料、皮蒽酮顏料、蒽嵌蒽醌顏料及二聘畊顏料、三芳基金 炭顏料和二酮Π比洛并。比略顏料。 ^進一步較佳作為有機著色劑的有花青素類、茜素、甜 菜素類 '墨水樹(haemat〇Xy1〇n)、葉綠素、洋紅、薑黃、血 紅蛋白、靛藍、蟲胭脂、散沫花、茜草、雷酷尼斯(Lackunis)、 胭脂樹紅、地衣紫色素、安帝克(編如〇、紫色及紅花色 素(safflor)。、 " 作為合適的合成有機著色劑,特別考慮具有與先前有 1 # Μ @似基礎之著色劑。更多細節可參考E.N.阿 200808878 布拉哈特(Abrahart)的烏門氏工業化學百科全書(uilmann,s Encyclopadia of Industrial Chemistry),第 9 冊,第 74-76 頁,VCH Verlagsgesellschaft mbH,魏因海姆,1987 ;,,染 料及其中間物”,第13-17頁,愛德華阿諾德有限公司 (Edward Arnold Ltd·),倫敦,,1977 ;及隆坡氏化學百科詞 典(Rompp’s Lexikon Chemie),第 10 版,第 1282-1283 頁, 鳩格西恩出版社(Georg Thieme Verlag),1997。 作為合適的有機著色劑種類(定位在著色結構單元的基 礎),提到的有亞硝基-、硝基-、單偶氮_、重氮、三偶氮·、 均一笨代乙浠…二苯基甲烷_、三芳基甲燒_、咕噸_、吖啶 -、喹啉-、噻唑…吲噠胺·、吖畊…腭畊…噻畊_、内酯_、 酞花青-著色劑。 在上述提及的有機及無機顏料當中,特別佳的有具有 BET表面積至少⑽平方公尺/克者,特別佳為至少平 ^公尺/克,而更佳為500平方公尺/克及最佳為至少1〇〇〇 _平方A尺/克者。此型式之顏料不僅能著色吸水性聚合物結 構,而且可額外有效地黏結討厭的臭味化合物,例如活性 碳。 來自上述提及的有機及無機著色劑為最佳活性碳,其 中再特別佳的是,此活性碳顆粒之平均顆粒直徑較佳位於 〇.〇1至_微米,特別佳從〇m〇〇微米及最佳從〇 25 至5 0微米的範圍内。 料水溶性聚合物⑴),諸如部分或完全4化的聚乙 "乙烯0比略烧_、殿粉類或澱粉衍生物之水溶性聚 17 200808878 =物醇類或Γ浠酸類可包含在、較佳係聚合至 捫兔kk些聚合物之分子量非為關鍵R,只要-’“溶性者。較佳的水溶性聚合物:匕 ==::合物,合‘二 k供作為欲聚合之單體的接枝基礎。 加劑⑽,較佳的是懸浮劑、臭 _ ( 以4),較佳係包含在聚合物結構中。 在根據本發明的聚合物結構之特別具 有至…量❶較佳至少7。重量%而更佳至少中9。二 =攜帶叛酸基團之單體為基礎。再者,根據本發明較: :疋組分⑷)由至少50重量%,較佳至少70重量% I组成’該酸較佳係㈣和到至少2G莫耳%,特別佳至少 5v莫耳%而更佳在從6〇至85莫耳%的範圍。 m =根據本發明之吸水性聚合物結構的較佳特徵為 下列性質之至少一種: ⑽著色劑的萃取’根據於本文描述之測試方法測定, 為每⑽克吸水性聚合物結構至乡01克,較佳為每⑽ 克吸水性聚合物結構至多〇 〇1克,特別佳為每⑽克吸水 性聚合物結構至多〇 〇〇1克; (β2)在頂部空間中的二甲基二硫醚之減少量,根據於 本文描述的測試方法測定,為至少8%,較佳為至少鄕 及特別佳為至少40% ; (β3) ΑΑΡ值,根據ERT (ERT=Ed嶋推薦的測試) 18 200808878 442.2-02在0.3磅/平方英寸壓力下測定(於微粒聚合物結構 之情況中,對總顆粒部分來說),為至少〗5克/克,特別佳 為至少20克/克及最佳為至少25克/克,其中aap值在〇.3 磅/平方英寸壓力下較佳不超過5〇克/克的值。 (β4) AAP值’根據ert 442.2-02在0.7碎/平方英寸 壓力下測定(在微粒聚合物結構的情況中,對總顆粒部分來 說),為至少12克/克,特別佳為至少15克/克及最佳為至 少18克/克’其中ΑΑΡ值在0.7磅/平方英寸壓力下較佳不 超過40克/克的值; (β5)-根據於本文描述的測試方法所測定之SFc值,Verlagsgesellschaft mbH, Weinheim, 995; W. Herbert's "Industrielle organische Pigmente", 2nd edition, pp. 482-485, VCH Verlagsgesellschaft mbH, Weinheim, 1995; W. Herb Sterling and K. Han Jue's Ρζ·gong, 2nd edition, p. 503, VCH Verlagsgesellschaft mbH.,, Heinheim, l"5; and W. Herbert and Κ········ Industrielle organische Pigmente,,, 箄 2, pp. 567-569, VCH Verlagsgesellschaft mbH, Weinheim, 1995. Particularly preferred organic pigments are azo pigments such as monoazo pigments, diazo pigments, beta-naphthol pigments, naphthol-AS-pigments, lacquered azo pigments, benzimidazolan pigments, diazo condensation Pigments, azo-metal complexes and isoindolinone pigments and isoporphyrin pigments. As suitable polycyclic pigments, there are mentioned phthalocyanine pigments, thioindigo pigments, and particularly preferred chinaeridon pigments and anthraquinone pigments and perin(n) pigments. More suitable polycyclic organic pigments are bismuth pigments such as pyrithione pigments, flavanone pigments, dermatan pigments, enamel pigments and two plucked pigments, Sanfang fund carbon pigments and diketone guanbyl. Than a little pigment. Further preferred as an organic colorant, anthocyanins, alizarins, beetins, ink trees (haemat〇Xy1〇n), chlorophyll, magenta, turmeric, hemoglobin, indigo, insect rum, halo, valerian , Lackunis, Rouge Red, Lichen Purple, Antec (such as 〇, purple and safflor), " as a suitable synthetic organic colorant, especially considering having 1 # with the previous Μ @Like basic coloring agent. For more details, please refer to EN A. 008808878, Abrahart, Uilmann, s Encyclopadia of Industrial Chemistry, Vol. 9, pp. 74-76. , VCH Verlagsgesellschaft mbH, Weinheim, 1987;,, Dyes and their intermediates, pp. 13-17, Edward Arnold Ltd., London, 1977; and the Longpo's Chemical Encyclopedia Dictionary (Rompp's Lexikon Chemie), 10th edition, pp. 1282-1283, Georg Thieme Verlag, 1997. As a suitable organic colorant species (positioned in a colored structure) The basis of the element), there are nitroso-, nitro-, mono-azo-, diazo, tris-azo, homo-phenylene, diphenylmethane, triarylmethyl ketone, 咕Tons of _, acridine-, quinoline-, thiazole, guanamine, sorghum, sorghum, sorghum, lactone, phthalocyanine-colorant. Among the above-mentioned organic and inorganic pigments, Particularly preferred are those having a BET surface area of at least (10) square meters per gram, particularly preferably at least flat square meters per gram, more preferably 500 square meters per gram, and most preferably at least 1 inch squared A square. The pigment of this type not only can color the water-absorbing polymer structure, but also can effectively bind an unpleasant odor compound such as activated carbon. The organic and inorganic colorants mentioned above are the best activated carbon, among which Even more preferably, the average particle diameter of the activated carbon particles is preferably in the range of 〇1 to _micrometers, particularly preferably in the range of 〇m 〇〇 micron and most preferably 〇25 to 50 μm. Polymer (1)), such as partially or completely 4-poly polyethylene "ethylene 0 than slightly burned _, temple powder or starch derivatives Poly 17,200,808,878 insoluble matter = Γ Hay alcohols or acids may be included in, preferably based polymer to the molecular weight of these polymers palpable rabbit kk is non-critical R, as long as - '' are soluble. A preferred water-soluble polymer: 匕 ==:: compound, which is a graft basis for the monomer to be polymerized. Additive (10), preferably a suspending agent, a odor (4), is preferably included in the polymer structure. The polymer structure according to the invention has, in particular, an amount of at least 7. % by weight and more preferably at least 9. Second = based on the monomer carrying the tickic acid group. Furthermore, according to the invention: 疋 component (4)) consists of at least 50% by weight, preferably at least 70% by weight of I. The acid is preferably (four) and at least 2G% by mole, particularly preferably at least 5 gram% by mole. And better in the range from 6〇 to 85mol%. m = a preferred feature of the water-absorbing polymer structure according to the invention is at least one of the following properties: (10) Extraction of the colorant 'as determined by the test method described herein, is (10) grams of water-absorbing polymer structure to the township 01 grams Preferably, each (10) grams of the water-absorbing polymer structure is up to 1 gram, particularly preferably up to 1 gram per (10) gram of the water-absorbing polymer structure; (β2) dimethyl disulfide in the headspace The amount of reduction, based on the test method described herein, is at least 8%, preferably at least 鄕 and particularly preferably at least 40%; (β3) ΑΑΡ, according to ERT (ERT=Ed嶋 recommended test) 18 200808878 442.2-02 is measured at a pressure of 0.3 psi (in the case of a particulate polymer structure, for the total particle fraction), at least gram 5 g/g, particularly preferably at least 20 g/g and most preferably At least 25 g/g, wherein the aap value is preferably no more than 5 g/g at a pressure of 〇3 psi. (β4) AAP value 'determined according to ert 442.2-02 at a pressure of 0.7 cc/in square (in the case of a particulate polymer structure, for the total granule fraction), at least 12 g/g, particularly preferably at least 15 G/g and optimally at least 18 g/g 'where the enthalpy value is preferably no more than 40 g/g at a pressure of 0.7 psi; (β5) - SFc determined according to the test method described herein value,
在根據ERT 441.2-02測定的>22克/克至£22克/克CRC 值下,為至少11〇χ1〇7立方公分秒/克,特別佳為至少 130χ10·7立方公分秒/克; -根據於本文描述的測試方法所測定之SFC值,At a CRC value of <22 g/g to £22 g/g as determined according to ERT 441.2-02, at least 11〇χ1〇7 cubic centimeters per gram, particularly preferably at least 130χ10·7 cubic centimeters per gram; - the SFC value determined according to the test method described herein,
在根據ERT 441·2_〇2測定的>22克/克至$24克/克CRC 值下,為至少90χ10·7立方公分秒/克,特別佳為至少 ΙΙΟχΙΟ·7立方公分克/克; -根據於本文描述的測試方法所測定之SFC值, 在根據ERT 441.2-02 (在對總顆粒部分測定的顆粒情 況中)測定的>24克/克至$26克/克CRC值下,為至少 70xl0·7立方公分秒/克,特別佳為至少90xl(T7立方公 分秒/克; -根據於本文描述的測試方法所測定之S F C值, 在根據ERT 441.2-02 (在對總顆粒部分測定的顆粒情 19 200808878 為至少 立方公 況中)測定的>26克/克至$28克/克CRC值下, 5 Ox 10-7立方公分秒/克’特別佳為至少7〇χΐ 〇·7 分秒/克; -根據於本文描述的測試方法所測定之值 在根據ERT 441.2-02 (在對總顆粒部分測定的顆粒情 況中)測定的>28克/克至$30克/克CRC值下,為至少 30xl(T7立方公分秒/克,特別佳為至少5〇xl〇j立 分秒/克; -根據於本文描述的測試方法所測定之SFc值, 在根據ERT 441.2-02 (在對總顆粒部分測定的顆粒情 況中)測定的>30克/克CRC值下,為至少1〇χ1〇_7立方 公分秒/克’特別佳為至少30x1 (Τ7立方公分秒/克。 根據本發明的聚合物結構之進一步較佳的具體實例具 有上述特徵(βΐ)至(β5)之任何可想見的組合,其中下列特徵 組合之具體實例較佳:⑽,)、^)、^)、^),^^)、 (β1)( β3)> (βΐ)( β4)> (βΐ)( β5)> (β!)( β2)( β3)> (β1)( β2)( β4) > (β1)( β2)( β5) ’其中(ρ1)、(β2)及(β1)( β2)為最佳的性質組 合。 才據本t明的聚合物結構之較佳的具體實例,就聚合 冓為ΛΚ 口物顆粒來說,這些可利用包含下列方法步驟 之方法獲得; a)攜帶酸某^ρ 圈之乙烯屬不飽和選擇性經部分中和的單 體於交聯齊j存太τ + 在下在水溶液中形成水凝膠之自由基聚合反 應; 20 200808878 b)乾燥水凝膠以獲得吸水性結構;及 Ο選擇性地吸水性聚合物顆粒之表面後交聯; 其中者色劑,較佳為作為著色劑之活性碳, i) 在自由基聚合反應之前或期間加至水溶液; ii) 在乾燥之前使其與水凝膠接觸,·或 出)在表面後交聯之前或期間使其與吸水性聚合物 接觸; 、"再 其中選擇i)及iii)特別佳。 藉由上述根據變化i)至iH)之著色劑的添加,確保著 色d不僅在聚合物顆粒的表面上局部化,而且均勻且均質 地分佈在顆粒内部。在變化Η)及Hi)中特別佳的是,凝膠 在與著色劑接觸之後進一步切碎一段足夠的時間,以使著 色劑能夠滲入凝膠中(變化η));或在後交聯期間,使用足 量的流體以使著色劑能夠滲入顆粒内部(變化出))。 根據本發明的聚合物結構之另一個較佳的具體實例, 鲁就聚合物結構為聚合物纖維來說,這些可利用包括下列方 法步驟之方法獲得: a)攜帶酸基團之乙烯屬不飽和選擇性經部分中和的單 體在水溶液中形成黏稠流體之自由基聚合反應,其中該水 溶液包含: -包含乙烯屬不飽和基團和可在加成反應中、在開環反 應中或在縮合反應中與單體之酸基團反應的官能基之交聯 劑;及/或 -包含二個可在加成反應中、在開環反應中或在縮合反 21 200808878 應中與單體之酸基團反應的官能基之交聯劑; b) 對該黏稠流體紡絲以獲得含水纖維; c) 藉由加熱至在從100至300°C,較佳150至25〇°C範 圍内之溫度來乾燥含水纖維,以獲得吸水性纖維; d) 選擇性地吸水性纖維之表面後交聯; 其中著色劑,較佳為活性碳, 0在自由基聚合反應之前或期間加至水溶液; ii)在含水纖維加熱之前使其與含水纖維接觸;或 β iii)在表面後交聯之前或期間使其與吸水性纖維接觸。At a CRC value of <22 g/g to $24 g/g as determined according to ERT 441·2_〇2, it is at least 90 χ10·7 cm 2 /g, particularly preferably at least ΙΙΟχΙΟ·7 cc/g; - the SFC value determined according to the test method described herein, under the CRC value of >24 g/g to $26 g/g measured according to ERT 441.2-02 (in the case of particles determined for the total particle fraction) At least 70 x 10 · 7 cubic centimeters per gram, particularly preferably at least 90 x 1 (T7 cubic centiseconds per gram; - SFC values determined according to the test methods described herein, in accordance with ERT 441.2-02 (determined in the total particle fraction) Particles of the situation 19 200808878 For at least cubic conditions, measured > 26 g / g to $ 28 g / g CRC value, 5 Ox 10-7 cubic centimeters / gram 'excellently at least 7 〇χΐ 〇 · 7 Minutes per gram; - values determined according to the test methods described herein are > 28 g/g to $30 g/g CRC as determined according to ERT 441.2-02 (in the case of particles determined for the total particle fraction) Lower, at least 30xl (T7 cubic centimeters per gram, especially preferably at least 5 〇 xl 〇 立 minutes/g; - according to this The SFc value determined by the described test method is at least 1 〇χ 1 〇 7 cubic centimeters at a CRC value of > 30 g/g as determined according to ERT 441.2-02 (in the case of granules determined for the total granule fraction) The second/gram' is particularly preferably at least 30x1 (Τ7 cubic centimeters per gram. Further preferred embodiments of the polymer structure according to the invention have any conceivable combination of the above features (βΐ) to (β5), wherein Specific examples of the following combinations of features are preferred: (10), ), ^), ^), ^), ^^), (β1) (β3) > (βΐ) (β4) > (βΐ) (β5)> (β!)( β2)( β3 )> (β1)( β2)( β4 ) > (β1)( β2 ) ( β5 ) ' where (ρ1), (β2) and (β1) (β2) are the most A good combination of properties. According to a preferred embodiment of the polymer structure of the present invention, in the case of polymerized ruthenium as the gargle particles, these can be obtained by a method comprising the following method steps; a) the vinyl group carrying the acid ρ loop is not Saturated Selectively Neutralized Monomers Crosslinked in a Hydrogenated Free Radical Polymerization Process in an Aqueous Solution; 20 200808878 b) Drying a hydrogel to obtain a water-absorbing structure; Surface cross-linking of the water-absorbing polymer particles; a toner, preferably activated carbon as a colorant, i) added to the aqueous solution before or during the radical polymerization; ii) before drying The hydrogel is contacted, or otherwise, in contact with the water-absorbing polymer before or during cross-linking of the surface; and "and among them i) and iii) are particularly preferred. By the addition of the above-described coloring agents according to the changes i) to iH), it is ensured that the coloring d is not only localized on the surface of the polymer particles but also uniformly and homogeneously distributed inside the particles. It is particularly preferred in the variations Η) and Hi) that the gel is further chopped after contact with the colorant for a sufficient period of time to allow the colorant to penetrate into the gel (variation η)); or during post-crosslinking A sufficient amount of fluid is used to allow the colorant to penetrate into the interior of the particle (change). According to another preferred embodiment of the polymer structure of the present invention, in the case where the polymer structure is a polymer fiber, these can be obtained by a method comprising the following method steps: a) Ethylene unsaturation carrying an acid group Selectively partially neutralized monomers form a free-radical polymerization of a viscous fluid in an aqueous solution, wherein the aqueous solution comprises: - comprising an ethylenically unsaturated group and which may be in an addition reaction, in a ring opening reaction or in condensation a crosslinking agent of a functional group reactive with an acid group of a monomer in the reaction; and/or - comprising two acids which may be combined with the monomer in the addition reaction, in the ring opening reaction or in the condensation reaction 21 200808878 a crosslinking agent for the reactive group of the group; b) spinning the viscous fluid to obtain an aqueous fiber; c) heating to a temperature in the range of from 100 to 300 ° C, preferably 150 to 25 ° C To dry the aqueous fibers to obtain water-absorbing fibers; d) to selectively cross-link the surface of the water-absorbing fibers; wherein the coloring agent, preferably activated carbon, is added to the aqueous solution before or during the radical polymerization; ii) In aqueous fiber plus Prior to contacting it with the aqueous fiber; or β iii) into contact with the rear surface of the absorbent fibers during or prior to crosslinking.
關於利用上述方法製造吸水性纖維之細節,可參考DE 690 28 341 T2、DE 692 23 953 丁1、DE 693 02 480 T2、DE 698 07 33 7 T2、DE 3 7 82 3 15 T2 及 DE 3 7 84 027 T3,其特別 關於製造纖維的方法或擠壓黏稠聚合物溶液之手段方面之 肩示藉此納入作為參考而代表本發明之揭示的部分。 同樣地,關於上述用來製造吸水性纖維的方法,藉由 φ 根據選擇丨)、Η)及in)加入著色劑之時刻,確保著色劑不 僅在聚合物纖維之表面上局部化,而且均勻地分佈在纖維 内部。 除了利用上述方法獲得之吸水性纖維之外,可例 由利用紡絲喷嘴擠壓包含有機溶劑、纖維素和吸水性 物顆粒之懸浮液及隨後將如此獲得的纖維傳輪至沉澱 仔之含纖維素纖維亦屬於根據本發明的吸水性聚合2 構。關於此製造方法的細節,可參考DE 1〇1 37 m 土 其關於含纖維素吸水性纖維之揭示藉此納入作為參考/ 22 200808878 成本毛月之揭不的部分。在⑻ 聚合物顆粒較佳為根 A1中所使用的 結構。再者,好之吸水性聚合物 之方法” 的疋根據可利用根據DE 101 37 17 之方法獲㈣根據本發明之吸水性纖維的特別且體 亚非或不僅使用根據本發明之吸水性(較佳只 結構作為吸水性顆 、、二者色)斌合物 顆粒,而且額外地將著色劑, 包含在吸水性聚合物顆粒中之著色劑,作為進::』For details on the production of water-absorbing fibers by the above method, reference is made to DE 690 28 341 T2, DE 692 23 953 ding 1, DE 693 02 480 T2, DE 698 07 33 7 T2, DE 3 7 82 3 15 T2 and DE 3 7 84 027 T3, which is particularly directed to the method of making the fibers or the means for extruding the viscous polymer solution, is hereby incorporated by reference. Similarly, with regard to the above-described method for producing water-absorbent fibers, it is ensured that the colorant is localized not only on the surface of the polymer fiber but also uniformly by the time of adding the colorant by φ), Η) and in). Distributed inside the fiber. In addition to the water-absorbent fiber obtained by the above method, for example, a suspension containing an organic solvent, a cellulose, and a water-absorbent particle is extruded by a spinning nozzle, and then the fiber thus obtained is transferred to the fiber of the precipitate. The fibril fibers also belong to the water-absorbent polymer structure according to the present invention. For details of this manufacturing method, reference may be made to DE 1〇1 37 m soil. The disclosure of cellulose-containing water-absorbing fibers is hereby incorporated by reference as part of the reference. The (8) polymer particles are preferably those used in the root A1. Furthermore, the method of the invention of the water-absorbing polymer can be obtained according to the method according to DE 101 37 17 (d). The water-absorbent fiber according to the invention is particularly and not only used or not only according to the water absorption according to the invention. The preferred structure is as a water absorbing particle, and both of them are conjugated particles, and additionally a coloring agent, a coloring agent contained in the water absorbing polymer particles, is used as:
組分加至包含有德、—^ 乍為進一步懸浮液 浮液,ίο 吸水性聚合物顆粒及纖維素的懸 ::、此上下文中,特別是上述已經在根據本發明 人7性聚合物結構之上下文中提及的那些著色劑較佳。 口適於製造著色纖維的進—步著色劑亦描述在觸 01/11121 Α1 中。 ’對上述提及目標之解決方法之進一步貢獻係藉由用來 製造著色吸水性聚合物結構之方法達成,_方法包括下列 方法步驟: _ a)攜f酸基團之乙烯屬不飽和選擇性經部分中和的單 體在水溶液中形成含水聚合物之自由基聚合反應; b) 藉由將聚合物加熱至在100至3〇〇〇c範圍内之溫度 來乾燥含水聚合物,以獲得吸水性聚合物結構; c) 選擇性地吸水性聚合物結構之表面後交聯; 其中著色劑,較佳為活性碳, i)在自由基聚合反應之前或期間加至水溶液; H)在乾燥之前使其與含水聚合物接觸;或 iii)在表面後交聯之前或期間使其與吸水性聚合物結構 23 200808878 接觸。 驚人但是仍然有利的是,已察覺到上述根據本發明的 吸水性(較佳經著色)聚合物顆粒可以著色劑之極低萃取能 力表現,因為用來著色的著色劑已經被加至單體溶液或作 用至尚未乾燥的水凝膠中及選擇性地聚合物隨後經表面後 交聯,以便著色劑半夾進聚合物内部中。若使用活性碳或 其它臭味黏結組分作為著色劑,根據本發明之方法其自身 的特徵亦在於這些組分之臭味黏結性質以完全出乎熟知人 士意料的方式並不會因為將此組分加入單體溶液中(方法變 化i)而不利地受影響。 若此方法應該提供微粒吸水性聚合物結構之製造,則 將上述提及作為組分(α3)的交聯劑加至單體溶液。在聚合 反應之後,於此情況中,獲得含水聚合物凝膠,然後將其 乾燥、粉碎及選擇性地表面後交聯。另一方面,若此方2 應該提供纖維狀吸水性聚合物結構之製造,則在單體溶液 中加入包含乙烯屬不飽和基團與可在加成、開環或縮合反 應中與單體之酸基團反應的官能基之交聯劑,及/或包含二 個可在加成、開環或縮合反應中與單體之酸基團反應的官 能基之交聯劑。於此情況中,聚合物之交聯已經不在聚合 期間發生,而是接著此聚合反應之後,在在1〇〇 j3〇(rc 間’較佳在150至250°C間之溫度乾燥期間進行。 較佳的著色劑及攜帶酸基團之乙烯屬不飽和選擇性經 部分中和的單體為上述已經關於根據本發明的聚合物結構 所提及作為著色劑(α4)及作為單體(α1)之那些著色劑及攜 24 200808878 帶酸基團之乙烯屬不飽和選擇性經部分中和的單體。 在方法步驟a)中使用的水性單體溶液除了作為溶劑之 水之外,較佳包含: (αΐ)乙烯屬不飽和攜帶酸基團之單體或其鹽類,其中 丙烯酸作為攜帶酸基團之單體特別佳; 、 (α2)選擇性地可與Ul)共聚合的單乙烯屬不飽和 體;The component is added to a suspension comprising a suspension, a suspension of the suspension, a water-absorbing polymer particle and a cellulose suspension:: In this context, in particular, the above-mentioned seventh polymer structure according to the present invention Those colorants mentioned in the context are preferred. The further step colorants suitable for the manufacture of colored fibers are also described in Touch 01/11121 Α1. 'The further contribution to the solution to the above mentioned objectives is achieved by the process used to make the colored water-absorbent polymer structure. The method comprises the following process steps: _ a) Ethylene-unsaturated selectivity of the acid-bearing group Free radical polymerization of a partially neutralized monomer to form an aqueous polymer in an aqueous solution; b) drying the aqueous polymer by heating the polymer to a temperature in the range of 100 to 3 〇〇〇c to obtain water absorption a polymer structure; c) a surface postcrosslinking of the selectively water-absorbing polymer structure; wherein the colorant, preferably activated carbon, i) is added to the aqueous solution before or during the free radical polymerization; H) before drying Contacting it with the aqueous polymer; or iii) contacting it with the water-absorbing polymer structure 23 200808878 before or during surface post-crosslinking. It is surprising, but still advantageous, that it has been observed that the above-described water-absorbing (preferably pigmented) polymer particles according to the present invention can be expressed by the extremely low extraction ability of the colorant since the coloring agent used for coloring has been added to the monomer solution. Or acting into the hydrogel which has not yet dried and optionally the polymer is subsequently post-crosslinked by surface so that the colorant is half-clamped into the interior of the polymer. If activated carbon or other odorous binder components are used as colorants, the method according to the invention is also characterized in that the odor-bonding properties of these components are completely unexpected to the well-known person and are not due to this group. Partitioning into the monomer solution (method change i) is adversely affected. If this method should provide for the production of a particulate water-absorbing polymer structure, the above-mentioned crosslinking agent as a component (?3) is added to the monomer solution. After the polymerization, in this case, an aqueous polymer gel is obtained, which is then dried, pulverized and selectively surface postcrosslinked. On the other hand, if the side 2 should provide the production of a fibrous water-absorbing polymer structure, the addition of an ethylenically unsaturated group to the monomer solution can be carried out in addition, ring opening or condensation reaction with the monomer. A crosslinking agent for a functional group reactive with an acid group, and/or a crosslinking agent comprising two functional groups reactive with an acid group of the monomer in an addition, ring opening or condensation reaction. In this case, the cross-linking of the polymer has not occurred during the polymerization, but is carried out after the polymerization, after drying at a temperature of between 1 and 3 Torr. Preferred color formers and ethylenically unsaturated selectively partially neutralized monomers bearing acid groups are those mentioned above as having a colorant (α4) and as a monomer (α1) with respect to the polymer structure according to the invention. Those colorants and monomers which are partially neutralized by the ethylenically unsaturated selectivity with an acid group. The aqueous monomer solution used in process step a) is preferably other than water as a solvent. The invention comprises: (αΐ) a monomer which is an ethylenically unsaturated acid group or a salt thereof, wherein acrylic acid is particularly preferred as a monomer carrying an acid group; and (α2) is selectively copolymerizable with U1) Unsaturated body;
:3)交聯劑,其中在製造聚合物顆粒的情況中,交聯 有至少二個乙烯屬不飽和基團的化合物較佳,而在 纖維製造的情況中’則加人包含乙烯屬不飽和基團及可在 加成、開環或縮合反應中與單體之酸基岐應的官能基之 交聯劑’及/或包含二個可在加成、開環或縮合反應中: 體的酸基團反應之官能基的交聯劑; 〃 (叫在方法變化〇的情況中,著色劑,較佳為活性碳; (α5)選擇性地水溶性聚合物;和 火 (α7)選擇性地一或多種添加劑。 。。作為可與UD共聚合的單乙烯屬不飽和單體,水 早體及添加劑,依次較佳為上述已經關於根據本發明之产 口物結構各別提及作為可與(α1)共聚合的單體、 性水合物及作為添加劑之那些化合物。 ,、 從上述提及的單體、共單體、交聯劑 及添加劑,吸水性平人礼^丨^ 丨王♦合物 l 永合物可利用不同的聚合方法來製造。 歹1 ,在此上下文中,應該提及的有本體聚合 揉捏器反應ϋ諸如擠壓器中進行,溶液聚合、噴霧 25 200808878 反相乳液聚合及反相懸浮聚合。 溶液聚合大概在作為溶劑之纟中進行。溶⑨聚合可連 續或不連續地進行。從先前技術已知有寬廣圍的變化可 能性,關於反應條件,諸如溫度、起始劑種類和量及反應 溶液。典型的方法描述在下列專利文件中:US 4,286,〇82、 DE 27 06 135 ^ US 4,076,663 > DE 35 03 458 > DE 40 20 780 > DE 42 44 548 > DE 43 23 001 ' Μ 43 33 056 ^ DE 44 1 8 8 1 8 〇: 3) a crosslinking agent in which, in the case of producing a polymer particle, a compound having at least two ethylenically unsaturated groups crosslinked is preferred, and in the case of fiber production, an addition of ethylene is unsaturated. a crosslinking agent and a functional group capable of reacting with an acid group of a monomer in an addition, ring opening or condensation reaction and/or comprising two in addition, ring opening or condensation reaction: a crosslinker of a functional group reactive with an acid group; 〃 (in the case of a process change ,, a colorant, preferably activated carbon; (α5) a selectively water-soluble polymer; and a fire (α7) selectivity One or more additives: as a monoethylenically unsaturated monomer copolymerizable with UD, water precursors and additives, preferably in the above, have been separately mentioned as relating to the structure of the mouthpiece according to the present invention. (α1) a copolymerized monomer, a hydrate, and those compounds as an additive. From the above-mentioned monomers, comonomers, cross-linking agents, and additives, water-absorbing flatness ceremony 丨^ 丨王♦ The compound 1 can be produced by different polymerization methods. In this context, mention should be made of bulk polymerization kneader reactions such as in an extruder, solution polymerization, spray 25 200808878 inverse emulsion polymerization and reversed phase suspension polymerization. Solution polymerization is carried out approximately as a solvent. The 9-polymerization can be carried out continuously or discontinuously. A wide range of variation possibilities are known from the prior art, with regard to reaction conditions such as temperature, type and amount of initiator, and reaction solution. Typical methods are described in the following patent documents. : US 4,286,〇82, DE 27 06 135 ^ US 4,076,663 > DE 35 03 458 > DE 40 20 780 > DE 42 44 548 > DE 43 23 001 ' Μ 43 33 056 ^ DE 44 1 8 8 1 8 〇
此些揭示藉此納入作為參考而因此形成本揭示的部分。 如知見瓜,聚合反應藉由起始劑起始。作為用來 起始聚合&應的起㈣,可使用|聚合反應條件下形成自 由基之全部起始劑,其通常用來製造超吸收劑。藉由電子 輻射在可聚合水性混合物上之效應來起始聚合反應亦可 能。聚合反應亦可在缺乏上述種類之起始劑下藉由於光起 始劑存在下的能量照射效應來起始。聚合起始劑可包括已 溶解或分散在根據本發明的單體溶液中。作為起始劑,考 慮分解成自由基且已為熟知技藝之人士已知的全部化合 物。這些特別包括已經在WO_A_2〇〇4/〇379〇3中提到作為 可能起始劑的那些起始劑。 特別佳的是,對吸水性聚合物結構之製造來說,使用 由過氧化氫、過氧二硫酸鈉及抗壞血酸組成的氧化還原二 統。 、’ 26 200808878 :可使用反相懸浮聚合及乳液聚合來製造聚合物結 劑之二這=法’將選擇性地包含水溶性聚合物及添加 )之水性經部分中和的溶液,藉助在疏 二:溶劑中之保護性膠體及/或乳化劑分散在疏水性有 溶及猎由自由基起始劑開始聚合反應。交聯劑可 性地在聚合期間加入。選擇性地,加:The disclosures of this disclosure are hereby incorporated by reference in their entirety in their entirety. As is known, the polymerization is initiated by a starter. As the starting material for the initiation of polymerization & (4), all of the initiators which form free radicals under polymerization conditions can be used, which are usually used to produce superabsorbents. It is also possible to initiate the polymerization by the effect of electron irradiation on the polymerizable aqueous mixture. The polymerization can also be initiated by the energy illuminating effect in the presence of a photoinitiator in the absence of the above-mentioned class of initiators. The polymerization initiator may include dissolved or dispersed in the monomer solution according to the present invention. As the initiator, all compounds which are decomposed into free radicals and are known to those skilled in the art are considered. These include, inter alia, those starting agents which have been mentioned as possible starters in WO_A_2〇〇4/〇379〇3. It is particularly preferred to use a redox system composed of hydrogen peroxide, sodium peroxodisulfate and ascorbic acid for the manufacture of the water-absorbing polymer structure. , ' 26 200808878 : Two-stage suspension polymerization and emulsion polymerization can be used to make a polymer-based solution. This method will selectively comprise a water-soluble polymer and a solution of the aqueous partially neutralized solution. Second, the protective colloid and/or emulsifier in the solvent is dispersed in the hydrophobic solution and the polymerization is started by the radical initiator. The crosslinking agent is optionally added during the polymerization. Optionally, add:
作為接枝基礎係經由單體溶液_由直^υ(α5) — 干版/合欣次糟由直接加入油相中來進 灯。现後,從混合物中共料移除水及過據出聚合物。 人中j在以聚合中及在反相懸浮聚合與反相乳液聚 5中一者,交聯可藉由在已溶解於單體 聯劑中聚合而谁并β ^ Τ扪夕吕月b又 聯劑與聚合物之官…=聚合步驟期間讓合適的交 --4,34〇,706 ;™ 37 13 601、DE 28 40 〇1〇 及 w〇_ 4中其相對應的揭示藉此納入作為參考。 八ictU a)中以溶液聚合或反相懸浮與乳液聚合獲得的 3水“物係在方法步驟b)中乾燥。 獲得水性聚合物顆粒的情況中’其中在聚合期間 又U '水㈣特別在溶液聚合的情況中 在乾燥之前先粉碎水凝膠。此粉碎係使用 = 所知的f碎裝置諸如絞肉器™sehwGlf,,)來進行: 水㈣之乾燥較佳在合適的乾燥器或 ;實:㈣的有旋轉管式烘箱、流化床乾燥器、二二 时U乾“或紅外線乾燥器。再者,根據本發明較佳 27 200808878 的是’在方法步驟b)中的水凝膠乾燥進行至水含量0.5至 25重量%,較佳從i至i 〇重 ^ . 室里/〇,其中乾燥溫度通常落在 從100至30CTC的範圍内。在 ^ 乾展之後,將聚合物顆粒粉 碎,選擇性地篩選及表面後交聯。 在製造吸水性聚合物纖維的情況中,在聚合之 得包含未交聯聚合物之黏稠溶液較佳藉由纺絲喷嘴擠壓: 且從此擠壓獲得的聚合物纖維然後純1〇〇至3〇〇 佳範圍從100至2〇(rc範 ㈤ 国円之/皿度下乾燥,其中此造成 來5物交聯及從而形成吸水性聚合物纖維。這些同樣可選 擇性地在進一步方法步驟中表面後交聯。 在後又%中,使已乾燥的聚合物結構或尚未乾燥但較 土已經粉碎的水凝膠與表面後交聯劑接觸,其巾使後交聯 3 ’特別是若其在後交聯條件下非液體者,較佳以包含後 入路劑和溶劑的流體形式各別與聚合物顆粒或與水凝膠接 觸1作為溶劑,較佳使用水、與水溶混的有機溶劑,諸如 :醇、乙醇、1-丙醇、2_丙醇或卜丁醇、或這些溶劑之至 種的此口物,其中水作為溶劑最佳。進一步較佳的是, 包含在流體中的後交聯劑之量範圍從5至75重量%,特別 佳為10 S 50重量%及最佳為15至4〇重量%,以流體的 總重量為準。 土使^ α物結構或粉碎的水凝膠各別與包含後交聯劑之 -接觸在根據本發明的方法中較佳藉由流體與聚合物 結構的良好混合來進行。 在根據本發明> 士1 α β , 月之方法中,係使聚合物結構在後交聯期 28 200808878 間較佳與至多20重量%,特別佳與至多15重量%,而更 佳與至多10重量% ’甚至更佳與至多5重量%及最佳與少 於3重量%的溶劑接觸,各別以聚合物結構之重量為準。As a grafting base, the lamp is fed directly into the oil phase via a monomer solution _ from υ (υ5) - dry plate / hexin. Thereafter, the water is removed from the mixture and the polymer is removed. In humans, in polymerization and in reversed-phase suspension polymerization and reversed-phase emulsion polymerization, cross-linking can be carried out by polymerizing in the monomer-linking agent, and β ^ Τ扪 吕 月 月The agreement between the agent and the polymer... = the appropriate disclosure of -4,34〇,706; TM 37 13 601, DE 28 40 〇1〇 and w〇_ 4 during the polymerization step Reference. The three water "systems obtained by solution polymerization or reverse phase suspension and emulsion polymerization are dried in the process step b). In the case of obtaining aqueous polymer particles, in which U 'water (four) is particularly In the case of solution polymerization, the hydrogel is pulverized prior to drying. This comminution is carried out using a known f-crushing device such as a meat grinder TMsehwGlf,,: water (4) is preferably dried in a suitable dryer or; Real: (4) There are rotary tube ovens, fluidized bed dryers, 22 hours U dry or infrared dryers. Furthermore, in accordance with the invention, preferably 27 200808878, the hydrogel drying in the method step b is carried out to a water content of from 0.5 to 25% by weight, preferably from i to i 〇. The drying temperature usually falls within the range from 100 to 30 CTC. After drying, the polymer particles are pulverized, selectively screened and surface postcrosslinked. In the case of producing a water-absorbing polymer fiber, the viscous solution containing the uncrosslinked polymer in the polymerization is preferably extruded by a spinning nozzle: and the polymer fiber obtained by extrusion is then purely 1 to 3 〇〇 范围 range from 100 to 2 〇 (rc ( (五) 円 / / 皿 干燥 drying, which causes the cross-linking of 5 substances and thus the formation of water-absorbing polymer fibers. These can also be selectively in further method steps Surface post-crosslinking. In the latter %, the dried polymer structure or the hydrogel which has not been dried but has been pulverized by the soil is contacted with the surface post-crosslinking agent, and the towel is post-crosslinked 3' especially if In the case of a non-liquid under post-crosslinking conditions, it is preferred to use a fluid comprising a post-entry agent and a solvent, respectively, in contact with the polymer particles or with the hydrogel as a solvent, preferably water, a water-miscible organic solvent. Such as: alcohol, ethanol, 1-propanol, 2-propanol or butanol, or such a solvent of these solvents, wherein water is most preferred as a solvent. Further preferably, it is contained in a fluid. The amount of postcrosslinker ranges from 5 to 75% by weight, especially 10 重量% by weight and preferably 15 to 4 重量% by weight, based on the total weight of the fluid. The soil or the hydrated hydrogel is separately contacted with the post-crosslinking agent. Preferably, the process of the present invention is carried out by a good mixing of the fluid with the polymer structure. In the method according to the invention > 1 α β , month, the polymer structure is compared between the post-crosslinking period 28 200808878 Preferably, up to 20% by weight, particularly preferably up to 15% by weight, and more preferably up to 10% by weight 'even more preferably up to 5% by weight and most preferably less than 3% by weight of solvent, each polymer The weight of the structure shall prevail.
合適於各別塗佈後交聯劑或包含後交聯劑的流體之混 合機組有例如Patterson_Kelley混合器、drais擾流混合 器、L^dige混合器、Ruberg混合器、螺旋混合器、平板混 合器及流化床混合器和連續操作型垂直混合器,其中藉由 旋轉刀以高頻混合聚合物結構之(Schugi混合器)。 作為在根據本發明之方法中使用的後交聯劑,應了解 較佳為包含至少二個可在縮合反應(=縮合交聯劑)中、在加 ^反應中或在開環反應中與聚合物結構之官能基反應的官 旎基之化合物,或能夠藉由在多價金屬陽離子與聚合物結 ,,官能基間的靜電交互作用來交聯聚合物結構的多價金 屬陽離子。作為在根據本發明之方法中較佳的後交聯劑有 在WO 2004/037903 A2中提到作為交聯劑類別π及IV之 交聯劑者。 在這t化合物當中,特別佳作為後交聯劑的為縮合交 :劑,諸如例如:二乙二醇、三乙二醇、聚乙二醇、甘油、 =甘油、丙一醇、二乙醇胺、三乙醇胺、聚氧丙烯、氧乙 虱丙烯嵌段共聚物或氧丙烯嵌段共聚物、脫水山梨糖醇 月曰肪自曰類、聚氧乙烯脫水山梨糖醇脂肪酸酯類、三羥甲基 …新戊四醇、♦乙稀醇、山梨糖醇、1,3 -二氧五環烧_ 酮(¼酸乙二酯)、4_甲基q,%二氧五環烷_2_酮(碳酸丙二 酉曰)4,5-—甲基-I,3-二氧五環烷_2-酮、4,4_二曱基-^^二 29 200808878 氧五環烷-2-酮、4-乙基-i,3-二氧五環烷冬酮、仁羥甲基·^3· 二氧五環烷-2-酮、1,3 -二氧六環烷·2_酮、4-甲基_1,3-二氧 六環烷-2-酮、4,6-二甲基-ΐ,3_二氧六環烷_2_酮和丨,3-二氧 五環烷-2-酮。 在已使聚合物結構各別與後交聯劑或與包含後交聯劑 的流體接觸之後’將它們加熱至在從4〇至300°C,較佳為 100至200 C及特別佳為150至250°C範圍内的溫度,以便,Mixing units suitable for the respective coated post-crosslinking agent or fluid comprising the post-crosslinking agent are, for example, Patterson_Kelley mixers, drais spoiler mixers, L^dige mixers, Ruberg mixers, spiral mixers, plate mixers And a fluidized bed mixer and a continuous operation type vertical mixer in which a polymer structure (Schugi mixer) is mixed at a high frequency by a rotary knife. As the post-crosslinking agent used in the process according to the invention, it is understood that preferably at least two can be polymerized in the condensation reaction (= condensation crosslinker), in the addition reaction or in the ring opening reaction. A functional group-reactive compound of a compound structure, or capable of cross-linking a polyvalent metal cation of a polymer structure by electrostatic interaction between a polyvalent metal cation and a polymer, functional group. Preferred postcrosslinkers in the process according to the invention are those which are mentioned in WO 2004/037903 A2 as crosslinkers for the crosslinkers of the classes π and IV. Among these compounds, particularly preferred as the post-crosslinking agent are condensed cross-linking agents such as, for example, diethylene glycol, triethylene glycol, polyethylene glycol, glycerin, =glycerol, propanol, diethanolamine, Triethanolamine, polyoxypropylene, oxyethylene propylene propylene block copolymer or oxypropylene block copolymer, sorbitan ruthenium saponin, polyoxyethylene sorbitan fatty acid ester, trishydroxymethyl... Neopentyl alcohol, ♦ ethylene glycol, sorbitol, 1,3-dioxapentanone (ethylene dicarboxylate), 4-methyl q, % dioxapentane-2 ketone ( Propyl hydrazide) 4,5-methyl-I,3-dioxopenta-2-ol, 4,4-diindolyl-^^29 200808878 Oxapentan-2-one, 4-ethyl-i,3-dioxo pentacyclobutanone, hydroxymethylmethyl·^3·dioxopenta-2-one, 1,3-dioxan-2-one, 4 -methyl-1,3-dioxan-2-one, 4,6-dimethyl-indole, 3-dioxan-2-one and indole-3-dioxapentane- 2-ketone. After the polymer structures have been individually contacted with the postcrosslinker or with the fluid comprising the postcrosslinker, they are heated to from 4 Torr to 300 ° C, preferably from 100 to 200 C and particularly preferably 150. To a temperature in the range of 250 ° C, so that
較佳的是藉此,聚合物結構之外部區域的交聯比内部區域 更強(=後交聯)。加熱處理的時間週期由想要的聚合物結構 之性為分佈曲線會由於加熱作用破壞的風險所限制。 在根據本發明之方法的另一個具體實例中,在使聚合 物結構之外部區域各別與後交聯劑或肖包含後交聯劑的流 體接觸之前或之後,較佳在之後,使其與包含鋁’較佳為 離子的化合物接觸。於此較佳的是,使包含量在 至30重量%之範圍内’特別佳的量範圍在從〇1至汕重 量%内及而更佳的量範圍錢〇.3至5重量%内(各別以聚 合物結構的重量為準)的銘之化合物與聚合物結構接觸。 使聚合物結構的外部區域與含紹化合物接觸,較 由在乾燥條件下混合聚合物結構與此化合物來進彳亍^ 由使聚合物結構與包含溶劑(較佳為水、與水溶混的有機二 劑如甲醇或乙醇或其至少二種 人 有機/合 -n接觸化合物的進 一體接觸’其中該使其接觸較佳係藉由將聚 與流體-起喷霧及結合來進行。在此上下文中粒 佳的是以二步驟方法使聚合物結構與包含含銘化合 30 200808878 觸。二步驟方法則包括第一混合,其中讓複數個聚合 物結構與流體結合;及第二混合,其中讓流體在聚合物結 構内均質化;其中在第一混合中,以使得各別聚合物結構 的動平均比在各別聚合物結構間之黏附能量大之速度來 混合聚合物結構;及在第二混合中,以比在第一混合中低 的速度混合聚合物結構。 藉由上述二步驟方法以包含含鋁化合物之流體來處理 _ w β物、°構’可獲得具有改良吸收性質之聚合物結構。 較佳的是,不考慮結晶水,含鋁化合物包含在進一步 流體中之量在從0·1至50重量%,特別佳在從1至30重 « %的範圍内,各別以進一步流體的總重量為準。再者較 仏的疋’使進一步流體以在0.01至15重量%範圍内之量, 特別佳在從0·05至6重量%範圍内的量與聚合物結構接 觸’各別以聚合物結構之重量為準。 • 車父佳的含銘化合物為含Al3 +離子化合物,諸如A1C13 · 鲁 6H2〇、NaAl(S04)2. 12H20、KA1(S04)2· 12H20 或 A12(S04)3 · ΐ4·18Η2〇之水溶性化合物;或不溶於水的鋁化合物,諸如 氧化銘類,例如αι2ο3或鋁酸鹽類。 根據本發明之方法,將著色劑加至水溶液或使其與含 水聚合物接觸,其中在使著色劑與含水聚合物接觸的情況 中’最好此發生在聚合物仍然具有至少5〇重量%水含量, 知'別佳為至少60重量%及而更佳為至少7〇重量%的時間· 點’各別以聚合物之總重量為準。 但是,著色劑亦可先在聚合物結構的表面後交聯期間 31 200808878 /人但疋’其中於此情況中’應該較佳地確保著色材料 可在聚合物結構之表面處理期間以足夠的程度滲入聚合物 結構内部中。 至單體溶液或以流體形式Preferably, the cross-linking of the outer region of the polymer structure is stronger (= post-crosslinking) than the inner region. The time period of the heat treatment is limited by the desired polymer structure as a distribution curve due to the risk of damage by heating. In another embodiment of the method according to the invention, before or after the external regions of the polymer structure are each contacted with the fluid of the post-crosslinking agent or the Schottky-containing postcrosslinker, preferably afterwards, A compound comprising aluminum 'preferably an ion is contacted. Preferably, the amount of the content in the range of up to 30% by weight is particularly preferably in the range from 〇1 to 汕% by weight and more preferably in the range of 〇3 to 5% by weight ( The compound of the name, which is based on the weight of the polymer structure, is in contact with the polymer structure. Contacting the outer region of the polymer structure with the compound containing the compound, and mixing the polymer structure with the compound under dry conditions to make the polymer structure and the solvent containing the solvent (preferably water, water-miscible) The two agents, such as methanol or ethanol, or the at least two human organic/in-n contact compounds, are in contact with each other, wherein the contacting thereof is preferably carried out by spraying and combining the polymerization with the fluid. In this context In the two-step method, the second step is to make the polymer structure and the inclusion of the inclusion of the combination of 200808878. The two-step method includes a first mixing in which a plurality of polymer structures are combined with the fluid; and a second mixing in which the fluid is allowed Homogenizing within the polymer structure; wherein in the first mixing, the polymer structure is mixed at a rate such that the moving average of the individual polymer structures is greater than the adhesion energy between the individual polymer structures; and in the second mixing The polymer structure is mixed at a lower speed than in the first mixing. The _w β material is obtained by treating the fluid containing the aluminum compound by the two-step method described above. A polymer structure having improved absorption properties. Preferably, the amount of the aluminum-containing compound contained in the further fluid is from 0.11 to 50% by weight, particularly preferably from 1 to 30% by weight, irrespective of the water of crystallization. Within the range, each is based on the total weight of the further fluid. Further, the 疋 疋 ' makes the further fluid in the range of 0.01 to 15% by weight, particularly preferably in the range of from 0. 05 to 6% by weight. The amount of contact with the polymer structure is determined by the weight of the polymer structure. • The car-containing compound contains a compound containing Al3 + ions, such as A1C13 · Lu 6H2〇, NaAl(S04) 2. 12H20, KA1 ( S04) 2·12H20 or A12(S04)3 · ΐ4·18Η2〇 a water-soluble compound; or a water-insoluble aluminum compound such as an oxidized class such as αι2ο3 or an aluminate. According to the method of the present invention, coloring Adding to the aqueous solution or contacting it with the aqueous polymer, wherein in the case of contacting the coloring agent with the aqueous polymer, it is preferred that the polymer still has a water content of at least 5% by weight, knowing that it is at least 60% by weight and more preferably at least 7 inches by weight The time and point 'each shall be based on the total weight of the polymer. However, the colorant may also be first crosslinked during the surface of the polymer structure 31 200808878 / person but in this case 'should be better' It is ensured that the coloring material can penetrate into the interior of the polymer structure to a sufficient extent during the surface treatment of the polymer structure. To the monomer solution or in the form of a fluid
J 較佳的是,將著色劑各別加 ^別L為以水溶液或水性分散液形式與水凝膠接觸。特別 疋幻吏用非水溶性顏料時,可加人合適的界面活性劑以確 -著色片!有足夠的为散度。但是,著色劑亦可選擇性地各Preferably, the colorants are separately added to form a contact with the hydrogel in the form of an aqueous solution or an aqueous dispersion. In particular, when using non-water-soluble pigments, you can add a suitable surfactant to make sure - the coloring sheet! There is enough divergence. However, the colorants can also be selectively
別:至早體溶液或以乾燥形式,較佳以著色劑粉末形式與 水滅膠接觸。 可利用根據本發明之方法獲得的較佳著色吸水性聚合 物結構較佳具有與上述根據本發明之較佳經著色之吸水性 聚合物結構相同的性質。 根據本發明的方法和根據本發明的聚合物結構之根據 具體實例,最好根據本發明僅提供下限之特徵值 :=表佳的下限值之20倍,較佳為1Q倍及特別佳為5 對上述目標的解決方法 進 ^ 步貝獻係藉由較佳荖备 該複合物包含根據本發明之吸水 根據本發明之方法獲得的各別吸水性聚合物 '、、。構及基材。於此較佳的是,根據本發明之 此緊緊地黏結。作為基材,聚合物如聚: 烯或“i胺之片材、金屬、非織物材料、毛絮…-丙 織材料、天然或合成纖維或其它料體較佳Y根攄I、編 進-步較佳的是’此複合物包括 :發明 L 31乾圍從約 32 200808878 10至100重量%,較佳約15至99 99重量%,特別佳從約 20至99重置%,而更佳從約25至95重量❼/❶及甚至更佳從 約50至90重量%之根據本發明之吸水性聚合物結構的區 域,各別以相關複合物區域之總重量為準,其中此區域較 佺具有至少〇·〇〇1立方毫米,較佳至少〇 〇ι立方毫米,而 更佳至少0.1立方毫米及最佳至少〇·3立方毫米的尺寸。 在根據本發明的複合物之特別佳的具體實例中,此為 _ 一種片狀複合物,如描述在WO-A-02/056812中作為,,吸收 材料”。WO-A-02/056812特別關於複合物的精確架構、每 單位面積其組分的質量和其厚度方面之揭示藉此納入作為 茶考而形成本發明之揭示的部分。 對上述目標之解決方法之進一步貢獻係藉由製造複合 物的方法達成,其中使根據本發明之吸水性聚合物結構或 可利周根據本發明之方法獲得的各別吸水性聚合物結構及 基材及選擇性地添加劑彼此接觸。作為基材,使用上述關 _ 於根據本發明之複合物已經提及的那些基材較佳。 對上述目標之解決方法之貢獻亦藉由可根據上述方法 獲得之複合物達成,其中此複合物較佳具有與上述根據本 發明之複合物相同的性質。 對上述目標之解決方法之進一步貢獻係藉由包含根據 本發明的吸水性聚合物結構或根據本發明之複合物的化學 產物達成。較佳的化學產物特別有泡沫體、成形物件、纖 維、片材、薄膜、電纜、密封材料、流體吸收衞生用品, 特別是屎布及衛生棉,植物或黴菌生長控制劑或植物保護 33 200808878 劑用之載體、建築材料用之添加劑 劑0Alternatively: to the early body solution or in dry form, preferably in the form of a colorant powder in contact with the water-killing gel. The preferred pigmented water-absorbing polymer structure obtainable by the process according to the invention preferably has the same properties as the preferred pigmented water-absorbing polymer structure according to the invention described above. According to a specific embodiment of the method according to the invention and the polymer structure according to the invention, it is preferred according to the invention to provide only the characteristic values of the lower limit: 20 times the lower limit value of the table, preferably 1Q times and particularly preferably 5 Solution to the above object Further, the composite comprises the respective water-absorbing polymer ', obtained by the method according to the invention, according to the invention, by means of a preferred preparation. Structure and substrate. Preferably, this is tightly bonded in accordance with the present invention. As a substrate, a polymer such as a polyene or "i-amine sheet, a metal, a non-woven material, a batt...-propane woven material, a natural or synthetic fiber or other material is preferably a Y-root, I-in- Preferably, the composite comprises: the invention L 31 dry circumference from about 32 200808878 10 to 100% by weight, preferably about 15 to 99 99% by weight, particularly preferably from about 20 to 99% by weight, and more preferably From about 25 to 95 weight ❼/❶ and even more preferably from about 50 to 90% by weight of the water-absorbent polymer structure according to the present invention, each of which is based on the total weight of the relevant composite region, wherein the region is The crucible has a size of at least 立方·〇〇1 mm 3 , preferably at least 立方m 3 mm, more preferably at least 0.1 mm 3 and most preferably at least 〇·3 mm 3 . Particularly preferred in the composite according to the invention In a specific example, this is a sheet-like composite, as described in WO-A-02/056812, an absorbent material. WO-A-02/056812, in particular with respect to the precise architecture of the composite, the mass per unit area of its components, and the thickness thereof, is hereby incorporated by reference as part of the disclosure of the present invention. A further contribution to the solution to the above object is achieved by a process for the manufacture of a composite, wherein the water-absorbent polymer structure according to the invention or the respective water-absorbent polymer structure and base obtainable according to the process of the invention The materials and optionally the additives are in contact with each other. As the substrate, it is preferred to use the above-mentioned substrates which have been mentioned in the composite according to the present invention. The contribution to the solution to the above object is also achieved by a composite obtainable according to the above method, wherein the composite preferably has the same properties as the composite according to the invention described above. A further contribution to the solution to the above object is achieved by a chemical product comprising a water-absorbing polymer structure according to the invention or a composite according to the invention. Preferred chemical products are, in particular, foams, shaped articles, fibers, sheets, films, cables, sealing materials, fluid-absorbent hygiene products, especially crepe and sanitary napkins, plant or mold growth control agents or plant protection 33 200808878 Used as carrier and additive for building materials
或土壤添加 出貢獻的有根據本發明之 之複合物在化學產物中, 特別在衛生用品如尿布或 顆粒作為植物或黴菌生長 返。在作為植物或黴菌生 載體的用途上,較佳的是 護活性物質可由載體控制 方法及非限制的實施例來Or the addition of the soil to which the composite according to the present invention is grown in chemical products, particularly in sanitary articles such as diapers or granules as plants or molds. In the use as a carrier for plants or molds, it is preferred that the active substance be controlled by a carrier and non-limiting examples.
亦對上述目標之解決方法做 吸水性聚合物結構或根據本發明 較佳在上述提及的化學產物中, 衞生棉中的用途,以及超吸收劑 控制劑或植物保護劑用載體的用 長控制劑或植物保護活性物質用 植物或彳放菌生長控制劑或植物保 釋放經過一段時間。 【實施方式】 本發明現在更嚴密地以測試 闡明。 測試方法 L^a,b色彩值之測暑 使用光暗色度计” ㈣(美國va瑞斯 通(Reston)的 Hunter Associates Laboratory)與下列設定進 行L,a,b色彩值之測定: “模式” 0/45 “區域視野(Area View)” 44·5毫米 “埠尺寸(Port Size)” 50.8毫米 “UV濾光器” 額定 在每次測量之前,校正LabScan ΧΕ,首先將屬於裝置 配件的黑色玻璃板夹鉗在樣品板與測量開口間,其中將玻 34 200808878 » 璃板放置在培養皿(直徑100毫米,深度:15毫米)上及藉 由啟動,,οκ”開關開始以黑色麵板校正。隨後,以相同^ 式’將自色標準板鋪在培養皿上及藉_啟動”〇κ,,開關進行 校正。 在已經進订杈正之後,按下,’讀取Std,,開關,以檢查 測量裝置的功能能力’其中標準板尚未移除。隨後,啟動: 讀取”開關以測量標準板的L,a,b值。 奴後,移除標準板及將培養皿填充以欲測量的吸水性 聚合物結構,其中以刮刀平順化產物表面。藉由按下,,讀取,, 開關來測量樣品。 1色劑之萃取能力的測定 在1,000毫升的玻璃燒杯中放置10克的吸水性聚合物 結構,且與750毫升0.9重量%已經帶至25t:的NaC1溶液 結合。然後,將玻璃燒杯放在磁攪拌器(IKA® Werke GmbH & C〇· KG, Staufen,德國,型號”rH basic 2”)上。然後, φ 將磁攪拌子(直徑〇·5公分,長度2公分)放在玻璃燒杯中 及在25 C下攪拌24小時,將旋轉速度設定為,,3”且排除光。 之後’在實驗室離心機(Sigma Laborzentrifugen GmbH,〇ster〇de am Harz,德國,型號” Sigma 2-16”含有 水平轉子4χ 1 〇〇毫升)中以2,000 rpm離心溶液。 然後測定著色劑在水性上層液中的量。若著色劑為水 溶性著色劑,可例如藉由UV-Vis光譜儀來進行水溶液中 著色劑量之測定,其中可使用合適的標準溶液來測定著色 材料濃度,因此用來定量著色劑之萃取量。若不溶於水的 35 200808878 著色劑包含在吸水性聚合物結構中時,萃取的著色劑量可 藉由將溶液蒸發及稱重剩餘的殘餘物來測定。 二甲基二硫醚之減少的测定 為了測定在頂部空間中的二甲基二硫醚之減少,將樣 品稱重至可密封的壓力取樣瓶中且與臭味物質的水溶液結 合。在室溫下等待與物質相依之時間後,在頂部空間取樣 器的烘箱中進行壓力取樣瓶回火。然後,將來自壓力取樣 瓶之頂部空間的樣品注入GC中。在下列提及的非極性毛 • 細管柱(其連接至FID)上進行分離。對減少之定量來說, 將樣品的臭味物質之波峰面積與不含臭味吸收劑的參考樣 品比較。 使用下列裝置: 10毫升頂部空間-壓力取樣瓶 鋁罩 密封鉗20毫米 開口甜20毫米 頂部空間取樣器: 氣相色層分析儀: 偵測器: 管柱: 幾何形狀: 製造商:Also for the solution of the above object, the water-absorbing polymer structure or the use of the above-mentioned chemical products, the use of the sanitary napkin, and the control of the carrier for the superabsorbent control agent or the plant protection agent according to the present invention. The agent or plant protection active is released over a period of time with a plant or a fungus growth control agent or plant. [Embodiment] The present invention is now more rigorously tested by testing. Test method L^a, b color value measurement using a light dark colorimeter" (4) (Hunter Associates Laboratory, Reston, USA) and the following settings for the determination of L, a, b color values: "mode" 0/45 “Area View” 44·5 mm “Port Size” 50.8 mm “UV Filter” Rated before each measurement, the LabScan is calibrated, first the black glass belonging to the device accessory Plate clamps were placed between the sample plate and the measurement opening, where the glass 34 200808878 » glass plate was placed on a Petri dish (100 mm diameter, depth: 15 mm) and by activation, the οκ" switch was initially calibrated with a black panel. Subsequently, the same standard is used to lay the self-color standard plate on the culture dish and the switch is used to calibrate the switch. After the order has been corrected, press , 'Read Std, switch, to Check the functional capabilities of the measuring device 'where the standard plate has not been removed. Then, start: read the switch to measure the L, a, b values of the standard board. After the slave, the standard plate was removed and the petri dish was filled with the water-absorbent polymer structure to be measured, wherein the surface of the product was smoothed with a spatula. The sample is measured by pressing, reading, and switching. Determination of the extraction ability of a toner A 10 g of a water-absorbent polymer structure was placed in a 1,000 ml glass beaker and combined with 750 ml of a 0.9 wt% NaC1 solution which had been brought to 25 t:. The glass beaker was then placed on a magnetic stirrer (IKA® Werke GmbH & C〇·KG, Staufen, Germany, model "rH basic 2"). Then, φ place the magnetic stirrer (5 cm in diameter, 2 cm in length) in a glass beaker and stir at 25 C for 24 hours, set the rotation speed to 3" and exclude the light. After 'in the laboratory Centrifuge the solution at 2,000 rpm in a centrifuge (Sigma Laborzentrifugen GmbH, 〇ster〇de am Harz, Germany, model "Sigma 2-16" containing horizontal rotor 4 χ 1 〇〇 ml). Then determine the amount of colorant in the aqueous supernatant If the colorant is a water-soluble colorant, the colorant amount in the aqueous solution can be determined, for example, by a UV-Vis spectrometer, wherein a suitable standard solution can be used to determine the coloring material concentration, and thus used to quantify the amount of colorant extracted. If the water-insoluble 35 200808878 colorant is included in the water-absorbing polymer structure, the extracted coloring dose can be determined by evaporating the solution and weighing the remaining residue. The reduction of dimethyl disulfide is determined in order to The reduction in dimethyl disulfide in the headspace was determined and the sample was weighed into a sealable pressure sampling vial and combined with an aqueous solution of odorous material. After waiting for the time dependent on the material, the pressure sample bottle is tempered in the oven of the headspace sampler. Then, the sample from the headspace of the pressure sampling bottle is injected into the GC. The non-polar hair column is mentioned below. Separation is carried out (which is connected to the FID). For the reduced quantitation, the peak area of the odorous substance of the sample is compared with the reference sample without the odor absorbent. The following device is used: 10 ml head space - pressure sampling bottle Aluminum cover sealing pliers 20 mm opening sweet 20 mm head space sampler: Gas chromatography: detector: column: geometry: manufacturer:
(例如HP零件編號:9301_0717) (例如HP零件編號·· 9301-0718) (例如HP零件編號:9301-0720) (例如HP零件編號·· 5181-1214) 惠普(Hewlett Packard)7694 惠普5890A FID RTX®5 (Crossbond®5%二苯基-95%二曱基聚矽氧烷) 60公尺χθ.53毫米xl.O微米 瑞斯泰克股份(有限)公司(Restek Corporation)(目錄編號:10258) 36 200808878(eg HP part number: 9301_0717) (eg HP part number · 9301-0718) (eg HP part number: 9301-0720) (eg HP part number · 5181-1214) HP (Hewlett Packard) 7694 HP 5890A FID RTX ®5 (Crossbond® 5% diphenyl-95% dimercapto polyoxyalkylene) 60 m χ θ.53 mm x l. O micron Restek Corporation (catalog number: 10258) 36 200808878
具有Turbochrom 4-軟體或同等 物的PC 評估系統: 製備20笔升大約50毫莫耳/升二甲基二硫醚在二甲基 甲酿胺中之原料溶液,且貯存在冰箱中有凸緣的2()毫升 頂部空間安瓿中。從此原料溶液,製備新鮮使用之濃度5〇 毫克/毫升的二甲亞砜水溶液。 在每個頂部空間壓力取樣瓶中各別稱取1⑽.〇毫克的 樣精確至0·1毫克)及藉由放置上凸緣罩覆蓋。在稱重 過程期間應該注意的是空氣無化學蒸氣。隨後,讓樣品與 2毛升新鮮製備的二甲亞硬水溶液結合及讓其在室溫下靜 置藉由電動依潘朵夫(Eppendorf)吸量管將2毫升的溶液 快速吸入頂部空間取樣瓶中。取樣瓶的凸緣罩僅有當從架 子取下對頂部空間取樣㈣行力K那點可舉起-段短的時 間以供吸量管吸取。取樣瓶應該藉由保持在架子中的凸緣 鉗直接凸緣化在連結器中。 間後’樣品以下列裝置設定開始。 烘箱溫度:451: 12〇t: 120°c 12·〇分鐘 60.0分鐘 〇·13分鐘 〇·02分鐘 0·02分鐘 在16小時之等待時 頂部空間: 迴線溫度:PC evaluation system with Turbochrom 4-software or equivalent: Prepare a raw solution of 20 liters of approximately 50 millimoles per liter of dimethyl disulfide in dimethylamine, and store in a refrigerator with a flange The 2 () ml head space is in the ampoule. From this raw material solution, a freshly used aqueous solution of dimethyl sulfoxide having a concentration of 5 毫克 mg/ml was prepared. Each of the headspace pressure sampling bottles was individually weighed 1 (10). The milligrams were accurate to 0.1 milligrams and covered by placing the upper flange cover. It should be noted during the weighing process that the air is free of chemical vapors. Subsequently, the sample was combined with 2 liters of freshly prepared dimethyl hard aqueous solution and allowed to stand at room temperature. 2 ml of the solution was quickly aspirated into the headspace sampling vial by an electric Eppendorf pipette. in. The flange cover of the sampling bottle can only be lifted for a short period of time for the suction of the suction tube when the top space is sampled from the frame (4). The vial should be flanged directly into the connector by a flange clamp held in the shelf. After the sample was started with the following device settings. Oven temperature: 451: 12〇t: 120°c 12·〇 minutes 60.0 minutes 〇·13 minutes 〇·02 minutes 0·02 minutes Waiting for 16 hours Headspace: Return temperature:
Tr·線溫度: GC循環時間: 取樣瓶平衡時間: 加壓時間: 迴線填充時間: 迴線平衡時間: 37 200808878 注入時間: 0·50分鐘 搖動: 關掉 載體壓力: 134千帕 取樣瓶壓力: 152千帕 應該注意的是, 烘箱溫度不超過45°C,否則應該冷卻 裝置。 使用氣相層析法在下列條件下,對在設定壓力取樣瓶 於頂部空間取樣器的烘箱中之溫度後所獲得的蒸氣相進行 測量: 溫度程式: 170°C 0 分鐘; -30°C /分鐘至ll〇°c 2分鐘 35°C /分鐘至250°C 2分鐘 注射器: 管柱流速:13毫升/秒 分流(沒有HS) : 0毫升/秒 分流(含有HS) ·· 150毫升/秒 管柱主要壓力:1〇〇千帕 對色5晋圖之評估來說’製備描緣在經鑑定取樣瓶輸入 後臭味物質之相對減少的excel表單。 SFC值之測宗 «描述在WO_A-95/22356中的方法進行在膨服狀態 下之渗透性(鹽液流動導電度=SFC)的測定。將〇.9克的超 吸收材料(總顆粒部分)稱入具有篩網底層之量筒中及小心 38 200808878 分佈在篩網表面上。讓超吸收材料在jAYCO合成尿中對 抗20克/平方公分之壓力膨脹一小時。在測量超吸收劑之 膨脹高度後,讓0.118M的NaCl溶液從標有刻度的貯存器 在固定的靜水壓力下流過膨脹的凝膠層。膨脹的凝膠層在 測量期間係覆蓋以特別的篩量筒,確保〇·118Μ的NaCl溶 液均勻分佈在凝膠上及在測量期間關於凝膠床性質方面的 固定條件(測量溫度20-25。〇。作用在膨脹的超吸收劑上之 壓力仍然為20克/平方公分。使用電腦及天平,在1 〇分鐘 之日守間週期内以20秒的區間測定為時間函數之通過凝膠 層之液體量。藉由回歸分析與梯度外插法來測定通過膨脹 的破膠層之流速(克/秒),及測定在2 - 1 〇分鐘内流動量於t=〇 的時間點處的中心點。SFC值(K)以立方公分秒克-1提供且 如下計算: κ = K (’ - 〇) · A — K (’= 〇) · 4 r-A^APl 139506 其中:Tr·Line temperature: GC cycle time: Sampling bottle equilibration time: Pressurization time: Return line filling time: Return line balance time: 37 200808878 Injection time: 0·50 minutes Shake: Turn off carrier pressure: 134 kPa sampling bottle pressure : 152 kPa should be noted that the oven temperature does not exceed 45 ° C, otherwise the device should be cooled. The vapor phase obtained after setting the temperature of the pressure sampling bottle in the oven of the headspace sampler was measured by gas chromatography under the following conditions: Temperature program: 170 ° C 0 min; -30 ° C / Minutes to ll〇°c 2 minutes 35°C / min to 250°C 2 minutes Syringe: Column flow rate: 13 ml / sec split (no HS): 0 ml / sec split (with HS) · · 150 ml / sec Main pressure of the column: 1 〇〇 kPa for the evaluation of the color 5 图 ' 'preparation of the relative decel form of the odor substance after the identification of the sample bottle input. The measurement of the SFC value «The method described in WO_A-95/22356 performs the measurement of the permeability (salt flow conductivity = SFC) in the expanded state. 〇.9 g of superabsorbent material (total particle fraction) was weighed into a graduated cylinder with a bottom layer of the screen and carefully placed on the surface of the screen at 38 200808878. The superabsorbent material was allowed to expand for one hour in a jAYCO synthetic urine against a pressure of 20 g/cm 2 . After measuring the expansion height of the superabsorbent, a 0.118 M NaCl solution was passed from the scaled reservoir through the expanded gel layer under a fixed hydrostatic pressure. The expanded gel layer was covered with a special sieve cylinder during the measurement to ensure that the NaCl solution of 〇·118Μ was evenly distributed on the gel and the fixed conditions regarding the properties of the gel bed during the measurement (measuring temperature 20-25. The pressure acting on the expanded superabsorbent is still 20 g/cm 2 . Using a computer and a balance, the liquid passing through the gel layer is measured as a function of time in a 20 second interval during the 1 〇 minute day interval. The flow rate (grams per second) through the expanded gel layer was determined by regression analysis and gradient extrapolation, and the center point at the time point of t = 〇 in 2 - 1 〇 minutes was determined. The SFC value (K) is provided in cubic centimeters per gram -1 and is calculated as follows: κ = K (' - 〇) · A - K ('= 〇) · 4 rA^APl 139506 where:
Fs(t=0)為流速,以克/秒計, L〇為凝膠層厚度,以公分計, R為NaCl溶液的密度(1.003克/立方公分), A為凝膠層在測量量筒中的上邊表面(28·27平方公分), ΔΡ為作用在凝膠片上之靜水壓力(492〇達因/平方公分), 及 Κ為SFC值[立方公分秒克-1]。 實施例 比較例: 39 200808878 由 3 00·〇 克丙烯酸、233.12 克 NaOH (50%)、430.12 克 去離子水、1.569克單烯丙基-聚乙二醇—750-單丙烯酸酯、 1186克聚乙二醇-300-二丙烯酸酯及6·〇〇克Bisomer®S10W (Cognis AG,德國)組成的單體溶液,藉由以氮除氣來釋放 出溶解的氧並冷卻至4 °C之開始溫度。在到達開始溫度之 後’加入起始劑溶液(〇·11克2,2,-偶氮雙-2-甲肺基丙烷-二 氯化氫在10.98克Ηθ中、0.3克過氧二硫酸鈉在9.70克 _ H2〇中、〇.〇7克35%過氧化氫溶液在1.93克H20中及0.015 克抗壞血酸在4.99克HA中)。在到達最後溫度約“它之 後’粉碎所形成的凝膠及在15〇°c下乾燥12〇分鐘。將乾 燥的聚合物粗糙地破碎,在切割研磨機SM100中研磨至小 於2,000微米之顆粒尺寸及篩選出具有15〇至85〇微米顆 粒尺寸之粉末。 實施例 1 ·· 、 遵循與比較例相同的程序,但是,其中彼此的差異為 φ 將以丙烯酸重量為準2重量%之活性碳(Fluka,p.a•粉末, 物件編號03 866,90%$53微米)加至單體溶液。 實施例2 : 遵循與比較例相同的程序,但是,其中彼此的差異為 將以凝膠重量為準2重量%之活性碳與切碎的凝膠混合。 在 合之後’將混合物精由絞肉器(“Fieischw〇lf”,克雷夫 特(Krefft)的商標,Typ AI2-3E含有5毫米孔洞板)切碎兩 次以均勻化,然後乾燥,粉碎及筛選。 實施例3 : 200808878 遵循與比較例相同程序,但是,其中彼此的差異為讓 以乾燥的吸水性聚合物重量為準〇·5重量%之工業碳黑 FW1P (來自Kalscheuren的Degussa)與乾燥的聚合物結合, 然後讓100克的此混合物在Krups授拌燒瓶中與總共4克 之1克碳酸乙二酯與3克水的水溶液結合,友在烘箱中於 180C下加熱30分鐘的時期。 對在比較例中及在實施例1至3中獲得之吸水性聚合 物結構來說,在頂部空間中二甲基二硫醚的減少係根據於 本文描述的測試方法測定。獲得下列結果(在表中所提供的 疋在頂部空間中二甲基二硫醚量的減少%,相關於在比較 例之έ有吸水性聚合物結構的頂部空間中所測量之二甲基 二硫鱗量): 貫施例 二甲基一硫醚量之減少[%ι 1 h-___一 23 2 3 _____一 49 在實施例1中獲得的聚合物為中灰色,而在實施例2 及3中獲得的超吸收劑為黑色產物。 實施例顯示,當使用活性碳時,臭味控制效應不會因 較強的黏結進人SAP中而減少,反而重要的是均勻分佈。 【圖式簡單說明】 (無) 【主要元件符號說明】 (無) 41Fs (t = 0) is the flow rate in grams per second, L 〇 is the thickness of the gel layer, in centimeters, R is the density of the NaCl solution (1.003 g / cm ^ 3 ), A is the gel layer in the measuring cylinder The upper surface (28·27 cm 2 ), ΔΡ is the hydrostatic pressure acting on the gel sheet (492 dynes/cm 2 ), and Κ is the SFC value [cubic centiseconds gram -1]. EXAMPLES Comparative Example: 39 200808878 From 30,000 gram acrylic acid, 233.12 grams NaOH (50%), 430.12 grams of deionized water, 1.569 grams of monoallyl-polyethylene glycol-750-monoacrylate, 1186 grams of poly A monomer solution consisting of ethylene glycol-300-diacrylate and bismuth Bisomer® S10W (Cognis AG, Germany), which releases dissolved oxygen by degassing with nitrogen and cools to 4 °C temperature. Add the starter solution after reaching the onset temperature (〇·11 g 2,2,-azobis-2-methyllungylpropane-dihydrogen chloride in 10.98 g Ηθ, 0.3 g sodium peroxodisulfate at 9.70 g _ H2 〇, 〇. 〇 7 g of 35% hydrogen peroxide solution in 1.93 g of H20 and 0.015 g of ascorbic acid in 4.99 g of HA). The resulting gel was comminuted at about the final temperature about "after it" and dried at 15 ° C for 12 minutes. The dried polymer was coarsely crushed and ground to a particle size of less than 2,000 microns in a cutting mill SM100. And screening powders having a particle size of 15 to 85 micrometers. Example 1 ··· Follow the same procedure as the comparative example, except that the difference between them is φ 2% by weight of activated carbon based on the weight of acrylic acid ( Fluka, pa•powder, item number 03 866, 90% $53 micron) was added to the monomer solution. Example 2: Follow the same procedure as the comparative example, except that the difference between them is 2 weights based on the weight of the gel. % of activated carbon is mixed with the chopped gel. After mixing, the mixture is refined from the meat grinder ("Fieischw〇lf", the trademark of Krefft, Typ AI2-3E contains 5 mm hole plate) Chop twice to homogenize, then dry, pulverize and screen. Example 3: 200808878 Follow the same procedure as the comparative example, except that the difference between them is based on the weight of the dry water-absorbing polymer. % of industrial carbon black FW1P (Degussa from Kalscheuren) was combined with the dried polymer, and then 100 grams of this mixture was combined in a Krups flask with a total of 4 grams of 1 gram of ethylene carbonate and 3 grams of water. The friend was heated in an oven at 180 C for a period of 30 minutes. For the water-absorbing polymer structures obtained in the comparative examples and in Examples 1 to 3, the reduction of dimethyl disulfide in the headspace was based on Determined by the test methods described herein. The following results were obtained (the % reduction in the amount of dimethyl disulfide in the headspace provided by the oxime provided in the table, related to the headspace of the water-absorbent polymer structure in the comparative example) The amount of dimethyl disulfide measured in the amount): the reduction of the amount of dimethyl monosulfide in the example [%ι 1 h-___123 2 3 _____ a 49 The polymer obtained in Example 1 It is medium gray, and the superabsorbents obtained in Examples 2 and 3 are black products. The examples show that when activated carbon is used, the odor control effect is not reduced by the stronger adhesion into the SAP, but instead It is important to distribute evenly. Ming] (none) [REFERENCE NUMERALS main element (None) 41
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WO2012163995A1 (en) * | 2011-06-01 | 2012-12-06 | Basf Se | Deodorizing mixtures for incontinence articles |
WO2013073614A1 (en) | 2011-11-15 | 2013-05-23 | 株式会社日本触媒 | Water absorbent composition and method for producing same, as well as storage and stocking method for same |
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US4342811A (en) * | 1979-12-28 | 1982-08-03 | Albany International Corp. | Open-celled microporous sorbent-loaded textile fibers and films and methods of fabricating same |
DE3545250A1 (en) * | 1985-12-20 | 1987-06-25 | Stockhausen Chem Fab Gmbh | Process for the production of water-swellable, water-insoluble synthetic fibres, and the use thereof as an absorption material |
DE4029591C2 (en) * | 1990-09-19 | 1995-01-26 | Stockhausen Chem Fab Gmbh | Process for the preparation of polymer-based absorption material with the addition of water-soluble substances and use of this absorption material for the absorption and / or subsequent release of water or aqueous solutions |
IL102338A (en) * | 1991-07-01 | 1996-11-14 | Du Pont | Polymeric febrids containing activated carbon |
DE19529348C2 (en) * | 1995-08-09 | 1997-11-20 | Stockhausen Chem Fab Gmbh | Absorbent for water and aqueous liquids based on polyacrylate and process for their production and use |
JPH0967522A (en) * | 1995-09-04 | 1997-03-11 | Sanyo Chem Ind Ltd | Production of water-absorbing resin |
JP3937549B2 (en) * | 1997-01-10 | 2007-06-27 | ソニー株式会社 | Method for producing water absorbent resin composition |
DE20121311U1 (en) * | 2000-07-21 | 2002-07-11 | The Procter & Gamble Company, Cincinnati, Ohio | Dark colored absorbent articles |
US6822135B2 (en) * | 2002-07-26 | 2004-11-23 | Kimberly-Clark Worldwide, Inc. | Fluid storage material including particles secured with a crosslinkable binder composition and method of making same |
DE202004015738U1 (en) * | 2004-10-12 | 2004-12-09 | Melitta Haushaltsprodukte Gmbh & Co. Kg | Absorption agent for absorption of moisture and odorous materials comprising mixture of active carbon and super absorber generally used for absorption of moisture and odors |
DE102005021221A1 (en) * | 2005-05-07 | 2006-11-09 | Geohumus International Gmbh & Co. Kg | Superabsorber with inorganic and organic ballast and additives |
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