TW201037000A - Flexible polyurethane low resilience foam and method for preparation - Google Patents

Flexible polyurethane low resilience foam and method for preparation Download PDF

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TW201037000A
TW201037000A TW98111033A TW98111033A TW201037000A TW 201037000 A TW201037000 A TW 201037000A TW 98111033 A TW98111033 A TW 98111033A TW 98111033 A TW98111033 A TW 98111033A TW 201037000 A TW201037000 A TW 201037000A
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isocyanate
weight
foam
parts
group
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TW98111033A
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TWI404739B (en
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Chung-Hsien Tu
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Chung-Hsien Tu
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Abstract

A novel flexible polyurethane low resilience foam based on reaction product of isocyanate-reactive composition with isocyanate composition is invented. The flexible polyurethane low resilience foam is prepared from reacting (a) isocyanate composition containing no aromatic isocyanate which has isocyanate group attaching directly to benzene ring, (b) isocyanate-reactive composition, (c) catalyst, and optionally (e) one or more ingredients selected from following: water, surfactants, cross-linkers and auxiliaries. The flexible polyurethane low resilience foam produced according to the preparation method has isocyanate index of from 75 to 105, density range of from 16 to 160 kilograms per cubic meter, and ball resilience of less than 15%.

Description

201037000 六、發明說明: 【發明所屬之技術領域】 本發明涉及脂肪族異氰酸酯和/或脂環族異氰酸酯和/或異氰酸酿基不 直接連接到苯環上的芳香族異氰酸酯基聚氨酯低回彈發泡體及其製備方 法。它還涉及可用於所述方法中的反應體系及具體異氰酸酯活性組分組合 物。 【先前技術】 軟質低回彈聚氨酯發泡體具有壓縮後緩慢、逐漸回復的特徵,通常稱 〇 為“慢回彈,,發泡體、“黏彈性,,發泡體、“死,’發泡體、“高阻尼,,發 泡體、形狀記憶”發泡體或“慢回復”發泡體。儘管其大多數物理性能 類似於常規聚氨酯發泡體,但低回彈發泡體的回彈性低許多,通常低於約 15%。 、、 低回彈聚氨酿發泡體具有優異抗衝擊性和優異減震性。它還具有形狀 調整和能量衰減特徵,使之成為理想的座墊材料。所述低回彈發泡體可用 於床塾、枕頭、汽車座墊和傢倶墊來減少壓力點,作為抗衝擊物用於運動 墊或頭盔。 〇 軟質低回彈聚躺發泡體具有_於人胸脯的«,因此可用于胸罩 塾和肩墊中。 通常低回彈聚氨泡體制多元醇共混物製備,所述多元醇共混物 包含當量低於450的硬質或半硬質三元醇和當量超過_的軟質三元醇。 大夕數軟貝低回彈聚氨醋發泡體在低異氰酸酿指數(異氰酸醋基與異氛酸 S旨雜基的莫耳比乘以則下製備。大多數情況下 ,該指數低於90。這 7高交聯、低分子量發趙聚合物’從而具有較低力學性能特別是撕 衣,度和伸長。還會導致窄操作範圍,通常引起發泡體收縮。因此通過調 t夕元醇、|►異紐s旨、表面潍劑、交聯劑、催化劑或其他添加劑的量 4 201037000 實用力學性能和可 和類型製備低贈聚IU旨發麵,以獲得具有低回彈 重現性生產特徵的發泡體。 美國專利7,38卿公開了採醜基值(多元醇中可反應的活性經基量 ㈣度’ ASTM D雜88中描述的方法)為5七邮的軟質多元醇 提供發泡體魏性並減少交聯,從而提高加工性能。 美國專利6,617,369中公開了類似方法。通過採用由環氧乙烧含量高達 5〇重量份(以励重量份總多元醇組合物計)多元醇組成的多元醇組合物可 衣備具有低回彈和提高的加工性能的發泡體。201037000 VI. Description of the Invention: [Technical Field] The present invention relates to an aromatic isocyanate-based polyurethane which is not directly bonded to a benzene ring by an aliphatic isocyanate and/or an alicyclic isocyanate and/or an isocyanate group. Foam and its preparation method. It also relates to the reaction system and specific isocyanate-reactive component compositions useful in the process. [Prior Art] Soft low-rebound polyurethane foam has the characteristics of slow and gradual recovery after compression, and is usually called "slow rebound, foam, "viscoelastic, foam, "dead," Foam, "high damping, foam, shape memory" foam or "slow recovery" foam. Although most of its physical properties are similar to conventional polyurethane foams, low rebound foam back Low elasticity, usually less than about 15%., Low resilience polyurethane foam has excellent impact resistance and excellent shock absorption. It also has shape adjustment and energy attenuation characteristics, making it an ideal seat cushion. The low resilience foam can be used for mattresses, pillows, car seat cushions and furniture cushions to reduce pressure points, and used as an impact resistant material for sports mats or helmets. It has been used in bras and shoulder pads. It is usually prepared from low resilience polyurethane foam polyol blends containing hard or semi-hard equivalents of less than 450 equivalents. Trihydric alcohol and soft triol with an equivalent weight exceeding _ The large-scale soft-shell soft-rebound polyurethane foam is prepared by multiplying the isocyanic acid-based index (the isocyanate group and the isocyanate S-based hetero group). In most cases, The index is below 90. These 7 highly crosslinked, low molecular weight polymers have a lower mechanical properties, especially tearing, elongation and elongation. They also result in a narrow operating range, which usually causes the foam to shrink. Adjust the amount of t-alcohol,|► 纽 s 、, surface tanning agent, cross-linking agent, catalyst or other additives 4 201037000 Practical mechanical properties and available types to prepare low-grant IU hair surface to obtain low back A foam that reproduces reproducible characteristics. U.S. Patent 7,38, discloses a ugly basis value (reactive reactive base amount in a polyol (four degrees)' method described in ASTM D Hybrid 88) The flexible polyol provides foaming properties and reduces cross-linking, thereby improving processability. A similar process is disclosed in U.S. Patent No. 6,617,369. a polyol composition composed of a polyol Having low rebound and improved foam processability.

美國專利6,39⑽描述了採賴均分子量(numW m〇iecuiar weight)超過約丨麟且絲值低於約56 mg K〇H/g的聚醋或聚環氧烧煙一 元醇和半硬質多元醇以獲得回彈性不到約15%,同時保持異氰酸醋指數超 過90的發泡體。 增塑劑的用途已有報導,如參見美國專利6,?9〇,871,其中採用函化石 壤'包含第-級羥基(Primaryhydr〇xylgr〇up’亦稱為伯羥基)的仰⑼脂肪 族聚合物及其混合物f備在寒冷氣釘具有良好柔祕的伽彈發泡體。 軟質聚氨酯低回彈發泡體首先於6〇年代中期首作為NASA (麗_ Aeronautics and Space Administmtion,美國航空與太空總署)的研究 技術項目喊果開發。該開發的目的旨在顧述低轉發顏重新分配在 起飛和降落過財Μ人受刺G力(G_F繼),並在長_行過程中提 供商業飛機飛行員更舒服的座席(參見如“ΙΝ·τ〇υαι”,第π卷第丨期第 1頁,2003年6月,聚氨醋發泡體協會(pFA)的定期出版物,ρ〇 Β〇χΐ459,U.S. Patent No. 6,39(10) describes poly- or polyepoxy-smoke mono- and semi-rigid polyols having a numW m〇iecuiar weight of more than about unicorn and a filament value of less than about 56 mg K〇H/g. A foam having a rebound resilience of less than about 15% while maintaining a isocyanate index of more than 90 is obtained. The use of plasticizers has been reported, see, for example, U.S. Patent No. 6, 〇, 871, in which the use of the functionalized rocky soil 'Yang (9) aliphatic containing a primary hydroxyl group (Primaryhydr〇xylgr〇up' also known as primary hydroxyl group) has been reported. The polymer and its mixture f are prepared in a cold gas nail with a good softness of the gauze foam. Soft polyurethane low resilience foam was first developed in the mid-1960s as a research project for NASA (Aeronautics and Space Administmtion). The purpose of the development is to address the low-transfer color redistribution in the take-off and landing of the wealthy people who are stabbed G-force (G_F following), and to provide a more comfortable seat for commercial aircraft pilots during the long-line process (see eg "ΙΝ · τ〇υαι", pp. π, vol. 1, p. 1, June 2003, regular publication of the Polyurethane Foam Association (pFA), ρ〇Β〇χΐ459,

Wayne, NJ)。不巧的是’由於其低指數性質和配製需要大量揮發性胺催化 劑,開發的低回彈發泡體釋放大量揮發性有機化合物(v〇c),從而妨礙其用 於密閉空間。從職彳4 ’其從未麟任何太雜或賴。 隨著近來越來越關心芳香族胺安全性,如作為由甲苯二異氰酸酯(tdi) 5 201037000 或二苯基甲烷二異氰酸酯(MDI)製備的聚氨酯發泡體的劣化反應產物的甲 笨二胺(TDA)和二胺基二笨曱烷(MDA) ’已開發多種合成方法來減少這種排 放。TDA和MDA為引起公眾關注的高毒性化合物和可能致癌物。美國專 利6,391,935(2002年5月21曰發佈,Bayer發明)進一步公開了“當採用甲 苯二異氰酸酯(TDI)在低指數下製備黏彈性發泡體時,所得發泡體會含不希 望的局含:E曱本·一胺’特別是在正常的硫化過程後”。 EUROPUR(歐洲軟質聚氨酯發泡體生產商協會,該協會成立於1966年) 於2007年宣佈了一項稱為“CertiPUR”的志願項目。CertiPUR為強調該工 〇 業承諾其產品安全、健康和環境(SHE)性能的項目。為了與CertiPUR標準 一致,對許多有害物質進行了限制或禁止。根據CertiPUR標準,聚氨酯發 泡體中的2,4-TDA和4,4’-MDA總量和HTDA和4,4,-MDA各自量的上 限為5ppm,以發泡體重量計。 歐盟於 2007 年6月 1 日正式實施 “REACH,,(Registrati〇nEvaluati〇nand Authorization of Chemicals,關於化學品註冊、評估、許可和限制)法案,對 以盟市場上和進入歐盟市場的所有化學品強制要求註冊、評估和許可,實 施安全監控。歐洲化學總署依據該法案第57條第丨項於2〇〇8年u月28 0 日公佈了 15 種尚度關切(SVHC ’ Substance of Very High Concern)物質,4,4, •MDA名列其一。 美國專利申請U.S.2005/0176838A1描述了採用包含至少一種經基值為 15-50 mg KOH/g的丙烯酸酯多元醇的多元醇組合物來減少氨基曱酸乙酯和 脲鍵的水解斷裂。該專利描述了”這種斷裂不僅在性能特徵明顯劣化,還會 產生芳香族胺,如f苯二胺(TDA)和二胺基二苯甲烷(MDA),,。 美國專利6,_,6G7細了將至少-種有機或錢贿加人異氰酸醋組 刀,然後使所得異氱酸酯組分與多元醇組分反應來製備軟質聚氨酯發泡體 的方法。所述聚氨酯發泡體中的酸酐進一步水解成相關酸,特別是在潮溼、 6 201037000 溫暖條件下。水職频啦鑛晴了發缝巾存麵财絲化劑, 因此阻止乱基曱_旨和/麵鍵在温暖、潮溼條件下再解離。不巧的是,由 於反應混合物愤度提高,這财法會降低錢自旨發泡體活性。由於其活 =低其僅可用於更具活性的芳香族異氰酸酿而不是脂肪族或脂環族異 氰酸酯反應。 採用上述處_齡缺.岐這猶難能鍵皿和福的形成, 而不能阻止這種芳香族胺的形成。美國專物⑽謂麵雙和美 ❹ 國專利6,_,術_的所有實施例報導了老化樣品中減少但仍高含量的 和A %使、,呈過特定的處理(參考該兩專利中說明的實施例,所 有發泡體樣品中的2,4韻* 4,4,德含量遠遠超 是Wayne, NJ). Unfortunately, due to its low index properties and the large amount of volatile amine catalyst required for formulation, the developed low resilience foam releases a large amount of volatile organic compounds (v〇c), which prevents it from being used in confined spaces. From the job 彳 4 ‘ it’s never been too much or too much. With the recent concern about the safety of aromatic amines, such as the methyl strepamine as a degradation reaction product of polyurethane foam prepared from toluene diisocyanate (tdi) 5 201037000 or diphenylmethane diisocyanate (MDI) TDA) and diaminodibenzane (MDA) have developed a variety of synthetic methods to reduce this emissions. TDA and MDA are highly toxic compounds and possible carcinogens of public concern. U.S. Patent 6,391,935 (issued May 21, 2002, issued by Bayer) further discloses that when a toluene diisocyanate (TDI) is used to prepare a viscoelastic foam at a low index, the resulting foam may contain undesirable stages. Contains: E 曱 · · an amine 'especially after the normal vulcanization process." EUROPUR (European Association of Flexible Polyurethane Foam Manufacturers, founded in 1966) In 2007, a voluntary project called "CertiPUR" was announced. CertiPUR is a project that emphasizes the industry's commitment to product safety, health and environmental (SHE) performance. In order to comply with the CertiPUR standard, many hazardous substances are restricted or prohibited. According to the CertiPUR standard, the upper limit of the total amount of 2,4-TDA and 4,4'-MDA and the amount of HTDA and 4,4,-MDA in the polyurethane foam is 5 ppm, based on the weight of the foam. On June 1, 2007, the European Union officially implemented the “REACH, (Registrati〇n Evaluati〇nand Authorization of Chemicals) Act, on all chemicals in the EU market and entering the EU market. Mandatory registration, evaluation and licensing, and implementation of safety monitoring. The European Chemicals Agency published 15 kinds of concern (SVHC ' Substance of Very High) according to Article 57 of the Act on April 28, 2008. Concerns, 4, 4, • MDA is one of the following. US Patent Application US 2005/0176838 A1 describes the use of a polyol composition comprising at least one acrylate polyol having a base value of 15-50 mg KOH/g. Reducing the hydrolytic cleavage of ethyl amino citrate and urea linkages. This patent describes "this fracture not only degrades significantly in performance characteristics, but also produces aromatic amines such as f-phenylenediamine (TDA) and diaminodiphenylmethane. (MDA),,. U.S. Patent No. 6, _, 6G7, a method for preparing a flexible polyurethane foam by at least one type of organic or money-added isocyanuric acid knives, and then reacting the obtained isophthalic acid ester component with a polyol component . The anhydride in the polyurethane foam is further hydrolyzed to the relevant acid, especially under humid conditions, 6 201037000. The water service frequency mine has cleared the hair towel to deposit the surface silking agent, thus preventing the chaos and the surface keys from dissociating under warm and humid conditions. Unfortunately, due to the increased indignation of the reaction mixture, this method will reduce the activity of the foam. Due to its low = low it can only be used for more active aromatic isocyanic acid rather than aliphatic or cycloaliphatic isocyanate reactions. It is difficult to prevent the formation of such aromatic amines by using the above-mentioned _ age-deficient 岐. All of the examples of U.S. patents (10), U.S. Patent No. 6, _, _ _ reported a reduction in the aging sample but still high content and A %, have been treated specifically (refer to the two patents In the example, the 2, 4 rhyme * 4, 4, and the content of all the foam samples are far beyond

CertiPUR標準中的上限)。 由於軟質聚旨低而發具有其他傳轉性發泡籍料無法替代 的獨特性能,因此發靴用料顧氰_來製備軟質聚氨醋低回 彈發續的方法’基於脂_和/或脂環族異驗_軟質聚躺低回彈發 泡體提供了針對這種需求的良好解決方法。 由於脂肪族和脂環族異氰_的活性低許多,它們極少用於製備聚氨醋 ❹發紐1中在健催化劑、更活性多異氰_組合物、高活性多元 醇的夕7L醇’、’_Εσ物或其他生產方法’選擇上開發了做少驗合成方法來 ‘備具有實用物理性能的脂肪族錢環顧鏡聚氨g旨發泡體。 美國專利巾π U.S.2_/〇ii4〇88公開了—種製傷軟質聚祕發泡體的 方法,所述方法包括在形成氨基甲酸乙_催化劑、發泡劑和泡泳穩定劑 存在下,在魏_指數超過9〇下0元醇混合物與多異氰_化合物反 應。所边多元醇混合物由多元醇⑷和多元醇⑻,一元醇⑼和任選多元醇 ⑹組成’多元醇⑻為聚•元醇’平均具有2_3個經基,經基值為雜哗 ΟΗ/g通物贱金屬魏姆合物催化_魏舰開環加成聚合到 7 201037000 挪财啦醇,懈有2~3舰,絲值為 多元醇丄平二:轉(D)為聚趟—元醇,經基值為_mgK〇H/g ; 醇,至多為整個多—Μ個經基經基值為脈1,830吨K〇H/g的多元 ^ MO 1〇%f * 〇The upper limit in the CertiPUR standard). Due to the low softness of the softness and the unique properties that cannot be replaced by other transferable foaming materials, the method of preparing soft polyurethane polyurethane with low recovery from the cyanide is based on fat_and/or fat. The ring-like test _ soft lie low-rebound foam provides a good solution to this need. Due to the low activity of aliphatic and cycloaliphatic isocyanide, they are rarely used in the preparation of polyamidoxime in the curing catalyst, more active polyisocyanate composition, and high activity polyol. The '_Εσ substance or other production method' has been developed to make a less-experimental synthesis method to prepare an aliphatic money ring with a practical physical property. U.S. Patent No. π US 2 _ 〇 ii 〇 〇 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 公开 , , , , , , , , , , , , The Wei_index exceeds 9〇 and the 0-alcohol mixture reacts with the polyisocyanate compound. The polyol mixture is composed of a polyol (4) and a polyol (8), a monohydric alcohol (9) and an optional polyol (6). The polyol (8) is a poly-alcohol having an average of 2 to 3 meridons and a base value of hydrazine/g.通 贱 贱 魏 魏 _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ Alcohol, the base value is _mgK〇H/g; alcohol, at most, the whole multi----------------------------------------------------------------------------

等異㈣二古 沒有針對這些職族和脂_二異驗S旨及XDI Ο ❹ 二異脈沾《接連接到苯環上的料㈣氰_,按照所述方法在任 ^風Μ缝製備中使㈣實蘭鱗細說明。事實上,餘 6曰’仍難以貫施所公開的多元醇混合物(參見以下對比實施例C1_C4)。 1992年9月15日頒布給M〇rim〇t。等的美國專利5,_7公開了採用 脂肪族多魏_旨棘物製财變黃聚氨缝的紐。崎方法包括 f C2-CH)賊的峡_或二缝環烯烴慨齡在下,使祕族多異氛 W曰預聚物與0.4-5倍於異氰酸醋當量的水反應。所述預聚物為通過平均分 子量為綱-5^0的多元醇與⑷6倍於祕當量的脂肪族多異氛酸醋, 以加成聚合獲得的脂肪顧氰酸酯封端預雜。所述脂肪族異氰酸醋的活 性通常低於芳香族異氛酸醋的活性。當脂肪族異氛酸醋變成預聚物時,分 子移動Itit纟下降’導致活性進一步減小。由於所得預聚物活性減小和 黏度高,Morimoto等的方法不能用於製備密度低於8〇公斤/立方公尺的聚 乳酯發泡體’且不能用於製備軟f聚氨g旨低回彈發泡體。 001年6月5日頒布給Du Prez等的美國專利6,2仏555描述了用 =度至v為900公斤/立方公尺(56pcf,碎/立方英尺)的微孔或無孔、光穩 定彈性、健或半㈣聚氨_反雜射難(舰)法。發财法包括:: 選自有機錯、有機叙和有機錫催化劑存在下,卿含量為购4%重 異佛爾S同二異氰酸醋三聚體/單體混合物與異氛酸醋活性組合物的反應。所 8 201037000 述異氰酸酯活性組合物包含(1)低不飽和度聚醚多元醇,如美國專利 5,470,813和美國專利5,498,583中所述,採用DMC(雙金屬氰化物)催化劑 - 製備,平均名義宫能度為2-4,平均當量為800-4,000 g/mo卜(2)約3-約20% 重量的至少一種增鏈劑,僅具有脂肪族或脂環族OH基作為官能團,官能 度為2,當量至多為80 g/m〇l,第一級羥基含量為至少50%和(3)約2-約10% 重量助催化劑體系,包含具有2-3個官能脂肪族NH、NH2或〇H基,且當 量至多為150 g/mol的催化劑’至少一種所述催化劑為第二級胺基(sec〇ndaty amino group ’亦稱為仲胺基)或第一級胺基(primary amin〇gr〇up,亦稱為伯 胺基)’且至少一種所述催化劑為胺引發催化劑。該發明提供了製備不變黃 〇 聚氨酯材料的方法,然而它僅能用於反應注射模塑法和緻密模塑部件生產。 2003年9月19曰公開、Mitsui-Takeda Chemicals Inc.的曰本專利申請jp 2003-261643A公開了製備脂環族多異氰酸酯基聚氨酯發泡體的方法。新型 (更昂貴且有限生產的)降冰片烷二異氰酸酯(2,5(2,6)-二(異氰酸根合甲基)雙 環[2.2.1]庚烧(產自 Mitsui-Takeda Chemicals Inc.的 “Cosmonate NBDI” 商 與聚趟多元醇及大量UV穩定劑一起反應,得到幾乎不變黃的聚氨酯發 泡體。沒有針騎彳!發紐力學性能的描述,沒有實_來說明其在軟質 低回彈聚氨酯發泡體製備中的用途。 〇 2006年9月28日公開、Kurashiki Boseki Corp.的日本專利申請jp 露257腦公開了製備衣服、保健或化妝品用的幾乎不變黃聚氣醋發泡 體的方法。所述聚氨自旨發泡體通過如下製備:使聚_元醇與多異氮酸酿 組合物反應,所述組合物包含(異佛爾酮二異氰酸醋(麵)和/或㈣三聚體 或其衍生物):(六亞甲基二異氛酸醋_1)的三聚體和/或胆衍生物)質量碉 節到(70-30):(30-70)的混合物。還解釋了:由於交聯增多,所得發泡體呈有 提高的發泡體硬度和低的渔壓縮變形。沒有針對多異氰酸醋組合物在軟質 低回彈發缝製财_途進挪述。_這些多異嫌敝合物製備的 軟質低回彈發泡體由於大量交聯而會是硬質的,因鱗致加工困難。此外, 9 201037000 由於這種三聚體及衍生物中異氰酸酯含量(NCO%)減少,與僅採用二異氰酸 酯相比,需要比採用脂肪族或脂環族二異氰酸酯高許多量的異氰酸酯混合 物來獲得任何指定的異氰酸酯指數。提高了這些聚氨酯發泡體的成本。増 加的異氰酸酯還意味著聚合物中硬鏈段增加,這會導致劣化加快。 2001年3月21日公開、INOAC MTP K.K.的日本專利申請JP 2001-72738A公開了具有優異耐水性且在陽光下不會變色的聚氨酯發泡 體’通過在選自二氮雙環烯烴或其苯基鹽的催化劑和弱酸的鹼金屬鹽存在 下,使脂肪族二異氰酸酯與環氧乙烧含量不到18重量份(以1〇〇重量份總 Q 多元醇環氧烷烴計)的多元醇反應。特別有用的是1,8-二氮雙環-(5,4,0)H —Equivalent (four) Ergu did not target these occupations and lipids _ two different test S and XDI Ο ❹ two different veins "connected to the benzene ring material (four) cyanide _, according to the method in the preparation of the wind quilting Make (4) Shilan scales detailed. In fact, it is still difficult to apply the disclosed polyol mixture (see Comparative Example C1_C4 below). Promulgated to M〇rim〇t on September 15, 1992. U.S. Patent No. 5, _7, et al., discloses the use of an aliphatic poly-wei. The Saki method consists of f C2-CH) thief's gorge or two-slit olefins are under the age, allowing the secret group to react with 0.4-5 times of isocyanate equivalents of water. The prepolymer is a fat-cyanate-terminated pre-mix obtained by addition polymerization, which is obtained by an average molecular weight of a polyol of the group -5 - 0 and (4) 6 times of a secret equivalent of an aliphatic polyisocyanate. The activity of the aliphatic isocyanic acid vinegar is generally lower than that of the aromatic oleic acid vinegar. When the aliphatic oleic acid vinegar becomes a prepolymer, the molecular movement Itit 纟 decreases, resulting in a further decrease in activity. Due to the reduced activity and high viscosity of the obtained prepolymer, the method of Morimoto et al. cannot be used to prepare a polylactide foam having a density of less than 8 〇 kg/m ^ 3 and cannot be used for the preparation of soft f-polyamide. Rebound foam. U.S. Patent No. 6,2,555 issued to Du Prez et al., issued June 5, 001, which describes the use of micro- or non-porous, light-stable, with a degree of v to 900 kg/m3 (56 pcf, broken/cubic feet). Elastic, healthy or semi-four (four) polyammonia _ anti-missing difficult (ship) method. The financing method includes:: selected from the group consisting of organic wrong, organic and organotin catalysts, the content of the 4% heavy isophora S isocyanate vinegar trimer/monomer mixture and sulphuric acid vinegar activity The reaction of the composition. 8 201037000 The isocyanate-reactive composition comprises (1) a low-unsaturated polyether polyol, as described in U.S. Patent No. 5,470,813 and U.S. Patent No. 5,498,583, which is incorporated by DMC (double metal cyanide) catalyst. 2-4, an average equivalent weight of 800-4,000 g/mob (2) of about 3 to about 20% by weight of at least one chain extender having only an aliphatic or alicyclic OH group as a functional group and having a functionality of 2, The equivalent weight is up to 80 g/m〇l, the first stage hydroxyl group content is at least 50% and (3) about 2 to about 10% by weight of the cocatalyst system, comprising 2-3 functional aliphatic NH, NH2 or 〇H groups And a catalyst having an equivalent weight of at most 150 g/mol 'at least one of the catalysts is a second-stage amine group (also known as a secondary amino group) or a first-stage amine group (primary amin〇gr〇up) Also known as primary amine groups' and at least one of the catalysts is an amine initiated catalyst. The invention provides a method of preparing an invariable xanthan polyurethane material, however it can only be used in reaction injection molding and compact molded part production. A method of preparing an alicyclic polyisocyanate-based polyurethane foam is disclosed in Japanese Patent Application No. JP-A-2003-261643A, the disclosure of which is incorporated herein by reference. Novel (more expensive and limitedly produced) norbornane diisocyanate (2,5(2,6)-bis(isocyanatomethyl)bicyclo[2.2.1] heptane (produced by Mitsui-Takeda Chemicals Inc. The "Cosmonate NBDI" quotient reacts with polyhydric hydrazine and a large amount of UV stabilizer to obtain a polyurethane foam that is almost indistinct yellow. There is no needle riding 彳! The description of the mechanical properties of the hair, there is no real _ to illustrate its softness Use of a low-rebound polyurethane foam in the preparation of a low-rebound polyurethane foam. The Japanese Patent Application jp 257, published by Kurashiki Boseki Corp., published on September 28, 2006, discloses an almost constant yellow polyglycol for the preparation of clothes, health care or cosmetics. A method of foaming the polyurethane foam by reacting a poly-alcohol with a polyisocyanuric brewing composition comprising (isophorone diisocyanate ( Surface) and / or (four) trimer or its derivatives): (trimethylene and / or cholesteryl derivatives of hexamethylene diiso- acetoacetate _1) mass 到 到 (70-30): ( A mixture of 30-70) also explains that the resulting foam exhibits improved foam hardness and low fishing compression deformation due to increased cross-linking. For the polyisocyanate vinegar composition in the soft low rebound elastic sewing _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ Difficulties in processing due to scales. In addition, 9 201037000 The reduction in isocyanate content (NCO%) in such trimers and derivatives is much higher than the use of aliphatic or cycloaliphatic diisocyanates compared to the use of diisocyanates alone. The isocyanate mixture to obtain any specified isocyanate index increases the cost of these polyurethane foams. The added isocyanate also means an increase in the hard segment of the polymer, which leads to accelerated deterioration. March 21, 2001, INOAC MTP Japanese Patent Application No. 2001-72738A to KK discloses a polyurethane foam having excellent water resistance and no discoloration under sunlight, by the presence of an alkali metal salt of a catalyst selected from diazocycloalkene or a phenyl salt thereof and a weak acid. The aliphatic diisocyanate is reacted with a polyol having an ethylene oxide content of less than 18 parts by weight based on 1 part by weight of the total Q polyol alkylene oxide. Is 1,8-diazabicyclo-(5,4,0)H —

碳烯-5 (DBU)、DBU 的苯基鹽、1,5-二氮雙環-(4,3,0)壬烯-5 (DBN)、DBN 的笨基鹽。由於這些非異氰酸酯活性二氮雙環烯烴的沸點低,如DBU的沸 點在532Pa的氣壓下僅為1〇〇〇c,這種催化劑將保留在成品發泡體中並逐漸 從發泡體中排放出來。從而,製備的聚氨酯發泡體具有大量v〇c排放。 2〇〇3年1月15日公開,INOAC MTP K.K.的日本專利申請jp 2003-012756A公開了採用脂環族二異氰酸酯與胺封端的多元醇反應製備 的,幾乎不變黃聚_發泡體。該巾請案還描述了僅由環氧峨單元組成 〇 的這些多元醇。這些胺封端聚環氧丙烷昂貴且僅有限供應,難以獲得有用 的月女封端聚環氧丙烷分子來製備軟質聚氨酯低回彈發泡體。 =此,需要開發軟質聚氨醋低回彈發泡體,所述軟質聚氨醋低回彈發 泡體今易通過採用脂肪族和/或脂環族二異氰酸g旨與市售可得的聚驗多元醇 反應製得’這種發泡體可在钱聚氨紐舰生產設壯製備,無需對設 備進行進一步改變。 【發明内容】 本發明-個目標是提供㈣健聚氨@旨伽彈發泡體的方法,所述軟質 聚氨醋低轉發泡縣於異_騎性組分錄林含異她旨基直接連 201037000 接到笨環上的芳香族異氰酸酯的異氰酸酯組分的反應產物。 本發明另一目標是提供一種新型異I酸酯活性組分組合物,所述組合物 適合與脂肪族和/或脂環族異氰酸酯和/或異氰酸酯基不直接連接到苯環上 的芳香族異氰酸酯,及一種或多種催化劑、水'作為泡孔調節劑的表面活 性劑’和其他添加劑反應製備軟質聚氨酯低回彈發泡體。 本發明另一目標是提供製備不變黃軟質聚氨酯低回彈發泡體的方法。 本發明另一目標是提供製備密度較低的不黃聚氨酯低回彈發泡體的一 步法。 Ο 本發明另一目標是提供製備模塑軟質聚氨酯低回彈發泡體的方法。 本發明另一目標是提供製備軟質聚氨酯低回彈發泡體的方法,所述軟質 聚氨酯低回彈發泡體在熱、潮濕環境下劣化時不會產生有毒芳香族胺。 本發明另一目標是提供製備軟質聚氨酯低回彈發泡體的方法,所述軟質 聚氨酯低回彈發泡體由不揮發性催化劑催化,釋放較少量的VOC。 本發明另-目標是提供製備聚氨醋低回彈發泡體的方法,所述聚氨醋低 畴發泡體在異氰酸酿指數為75德下,具有提高的力學性能,特別是撕 ^ 裂強度’拉伸強度和伸長。 本發明另-目標是提供-雛f聚錢低轉發·,所絲f聚氣醋 低回彈發泡_伽彈和咖性倾,而沒有賴增賴,且在溫度變化 下顯示很小的硬度變化,同時具有高透氣性。 本發明另目;^提供細可再生生物源多元醇,製触物可降解聚氨 酯低回彈發泡體的方法。 本發明另-目標是提供新财變黃聚錢翻泡體,所述聚細旨低 回彈發泡體可用於胸罩塾、肩塾、床墊、枕頭、家具塾和汽車坐塾領域。- 201037000 本發月另目標是提供採用較少量或不採用常規和/或活性第三級胺 (tertiary amine ’亦稱為叔胺)催化劑,製備聚氨醋發泡體,以減少汽車内部 - 霧化的方法。 本毛月個實知方案公開了-種軟質聚氨醋低回彈發泡體。本發明軟質 聚氨醋低回彈發泡體包含以下物質的反應產物: 種”氰S夂Sg組分,所述異氰酸醋組分基本不含異氰酸醋基直接連接到 苯環上的芳香族異氰酸酯; 〇 _種錄_旨雜齡物,舰異驗麟舰合物包含: (bl)第-異氰酸醋活性組分,具有至少μ個異氮酸醋活性基、優選為 2·6·6.5個異氰酸酯活性基、更優選為2.65-6.0個異氰酸酯活性基、最優選 為2’7 5.5個異氰酸醋活性基,經基當量低於800、優選為80-800、更優選 為1〇〇_7〇〇、最優選為110_600,經基值高於7〇mgKOH/g、優選為7〇-7〇〇mg KOH/g、更優選為8〇_56〇 mg K〇H/g、最優選為吨奶敗, (b2)第二異氰酸酯活性組分’平均羥基官能度低於6.0、優選為1.8-6.0、 更優選為1.85-4.5,羥基當量為600-6,000、優選為7〇〇-5,000、更優選為 ❹ 800-4,500 ’經基值為9-94 mg KOH/g、優選為19-80 mg KOH/g、更優選為 14^70mgK〇H/g’第一級羥基含量為至少3〇重量份、優選至少4〇重量份、 更優選至少51重量份’以所述第二異氰酸酯活性組分羥基總重量為100重 量份計, 其中所述第一異氰酸酯活性組分的使用量為20-90重量份,優選20-70 重里份’所述第二異氰酸酯活性組分的使用量為10-80重量份,優選30-80 重量份’都以10〇重量份所述異氰酸酯活性混合物計; 催化密 "i k地種或多種選自以下的物質··水、表面活性劑、交聯劑及添加劑; 12 201037000 所述任選的交聯劑的重均分子量為60-420 g/m〇l並具有至少兩個異氰 酸酯活性官能團;其中如果使用,所述交聯劑的使用量為〇2_15重量份、 最優選1.2-12重篁份,以1〇〇重量份所述異氰酸g旨活性混合物計。 其中所述發泡體在異氰酸酯指數為75-105下製備。 任選,所述異氰酸酯活性組分還包含0·4〇重量份(以1〇〇重量份異氰酸 酯活性組分計)聚合物多元醇,所述聚合物多元醇的固含量為5_55重量份(以 1〇〇重量份聚合物多元醇計),羥基值為i5_50mgKOH/g。Carbene-5 (DBU), a phenyl salt of DBU, 1,5-diazabicyclo-(4,3,0)nonene-5 (DBN), a stupid base of DBN. Since these non-isocyanate-reactive diazabicycloolefins have a low boiling point, such as a boiling point of DBU of only 1 〇〇〇c at a pressure of 532 Pa, the catalyst will remain in the finished foam and gradually discharge from the foam. . Thus, the prepared polyurethane foam has a large amount of v〇c emissions. Japanese Patent Application No. 2003-012756A to INOAC MTP K.K. discloses a nearly invariant yellow poly-foam prepared by reacting an alicyclic diisocyanate with an amine-terminated polyol. The towel also describes these polyols which consist solely of oxime units. These amine-terminated polypropylene oxides are expensive and limited in supply, making it difficult to obtain useful moon-capped polypropylene oxide molecules to prepare flexible polyurethane low resilience foams. = This requires the development of a soft polyurethane low resilience foam, which is readily available commercially by the use of aliphatic and/or alicyclic diisocyanate. The obtained polyphenol reaction was made to produce 'this kind of foam can be produced in the production of the money polyurethane ship, without further changes to the equipment. SUMMARY OF THE INVENTION The present invention is directed to a method for providing (4) a viscous polyaluminum sulphide low-foaming foaming county. Even 201037000 receives the reaction product of the isocyanate component of the aromatic isocyanate on the stupid ring. Another object of the present invention is to provide a novel iso-Iester active component composition which is suitable for aromatic isocyanates which are not directly bonded to the benzene ring with aliphatic and/or alicyclic isocyanate and/or isocyanate groups. , and one or more catalysts, water 'surfactant as a cell regulator' and other additives are reacted to prepare a flexible polyurethane low resilience foam. Another object of the present invention is to provide a process for preparing an invariable yellow flexible polyurethane low resilience foam. Another object of the present invention is to provide a one-step process for preparing a low density non-yellow polyurethane low resilience foam.另一 Another object of the present invention is to provide a process for preparing a molded flexible polyurethane low resilience foam. Another object of the present invention is to provide a process for producing a flexible polyurethane low resilience foam which does not produce a toxic aromatic amine when degraded in a hot or humid environment. Another object of the present invention is to provide a process for preparing a flexible polyurethane low resilience foam which is catalyzed by a non-volatile catalyst to release a relatively small amount of VOC. Another object of the present invention is to provide a method for preparing a polyurethane foam low resilience foam having improved mechanical properties, particularly tearing, at an isocyanic brewing index of 75 de. ^ Crack strength 'tensile strength and elongation. Another object of the present invention is to provide - a small f-collecting low-transfer, a low-rebounding foaming _ _ 弹 弹 and _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ The hardness changes while having high gas permeability. The present invention is directed to a method of providing a fine regenerable biological source polyol and a primer-degradable polyurethane low resilience foam. Another object of the present invention is to provide a new financially-reversed low-rebound foam which can be used in the fields of bras, shoulder blades, mattresses, pillows, furniture, and car seat. - 201037000 Another objective of this month is to provide polyurethane foams with less or no conventional and/or active tertiary amine (also known as tertiary amine) catalysts to reduce the interior of the car - The method of atomization. This Maoyue know-how program discloses a kind of soft polyurethane low resilience foam. The soft polyurethane low resilience foam of the present invention comprises the reaction product of the following: a "Cyanide S?Sg component, the isocyanate component is substantially free of isocyanate groups and is directly attached to the benzene ring. Aromatic isocyanate; 〇 _ _ _ _ 杂 杂 旨 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰 舰2·6·6.5 isocyanate reactive groups, more preferably 2.65-6.0 isocyanate reactive groups, most preferably 2'7 5.5 isocyanate active groups, base equivalent weight less than 800, preferably 80-800, more It is preferably 1〇〇_7〇〇, most preferably 110_600, and has a base value of more than 7〇mgKOH/g, preferably 7〇-7〇〇mg KOH/g, more preferably 8〇_56〇mg K〇 H/g, most preferably ton of milk, (b2) second isocyanate active component 'average hydroxy functionality of less than 6.0, preferably 1.8-6.0, more preferably 1.85-4.5, hydroxyl equivalent of 600-6,000, preferably It is 7〇〇-5,000, more preferably ❹800-4,500′, the base value is 9-94 mg KOH/g, preferably 19-80 mg KOH/g, more preferably 14^70 mg K〇H/g' first Hydroxyl content At least 3 parts by weight, preferably at least 4 parts by weight, more preferably at least 51 parts by weight 'based on 100 parts by weight of the total weight of the second isocyanate active component hydroxyl group, wherein the first isocyanate active component is used 20 to 90 parts by weight, preferably 20 to 70 parts by weight 'the second isocyanate-reactive component is used in an amount of 10 to 80 parts by weight, preferably 30 to 80 parts by weight, to 10 parts by weight of the isocyanate-active mixture Catalyzed "ik species or a plurality of materials selected from the following: water, surfactants, crosslinking agents and additives; 12 201037000 The optional crosslinking agent has a weight average molecular weight of 60-420 g/ M〇l and having at least two isocyanate reactive functional groups; wherein, if used, the crosslinking agent is used in an amount of from 2 to 15 parts by weight, most preferably from 1.2 to 12 parts by weight, based on 1 part by weight of the isocyanate The foam is prepared at an isocyanate index of 75 to 105. Optionally, the isocyanate active component further comprises 0.4 parts by weight (in 1 part by weight of the isocyanate active component). Polymer polyol The polymer polyol has a solid content of 5 to 55 parts by weight based on 1 part by weight of the polymer polyol, and a hydroxyl value of i5 to 50 mgKOH/g.

所述異氰酸酯活性组分可包含〇_5.〇重量份,優選為〇_3 5重量份(以1〇〇 重量份總發泡體質量計)聚環氧丙烧㈣作為開孔冑,所述聚環氧丙燒㈣ 的名義羥基官能度為1,重均分子量為800_8,500g/m〇1。 本發明另-實财案涉及製備軟質職隨轉發缝的方法。本發明 方法包括製備發泡體製劑,所職劑包含異氰_活性混合物、基本不含 異氰酸喊直接連_笨環上的異驗自旨的異紐敝分、水、催化劑以 在發泡體配方巾職氨基甲酸酯鍵和泡沫穩定赚面雌劑,然後發泡, 之後將所得發顏製_化。所述異驗騎性混合物選自上述異氣酸酷 活性混合物。The isocyanate-reactive component may comprise 〇_5. 〇 by weight, preferably 〇_3 5 parts by weight (based on 1 gram by weight of the total foam mass) of polyglycidone (4) as an open cell, The polyglycolide (IV) has a nominal hydroxyl functionality of 1 and a weight average molecular weight of 800_8,500 g/m〇1. The invention of the present invention relates to a method for preparing a soft job with a forwarding seam. The method of the invention comprises preparing a foam preparation, the agent comprising an isocyanide-active mixture, substantially free of isocyanic acid, direct-connected, and the like, a water, a catalyst, The blister formula towel urethane bond and the foam stabilizes the face female agent, and then foams, and then the resulting hair is made into a scent. The heterochiral mixture is selected from the above-described isogasoic acid active mixture.

本發明另一實施方案涉及通過採用 體的方法。 一步法製備軟質聚胺酯低回彈發泡 本發明另一實施方案涉及通過上述方法製備、紐為丨㈣公斤/立方 米的軟質聚氨酯低回彈發泡體。 本發明另4財録及製備敕質模《氨峨_發泡體的方法。 =發刪聚她回彈發泡體製備中,不需要對現有議發 產设備進行特殊改變。 本發明異氰義活性組合物錢大密度和硬度範_軟«氨醋低回 13 201037000 彈發泡體製備中提供更大配方組分範圍。 【實施方式】 本發明涉及新型軟質聚氨酯低回彈發泡體,通過使基本不含異氰酸酯美 直接連接到苯環上的料族異氰_旨的異氰酸敝分與已公開異氰酸自旨活 性組分及催化劑、任勒水、表面活測、交聯劑和添加劑反應來製備。 所述異氰酸酯紅分選自一種或多種以下的異氰酸酯:脂肪族異氰酸酯、 脂環族異氰酸酯和異氰酸酯基不直接連接到笨環上的芳香族異氰酸酯。當 使用脂肪族和/或脂環族和/或異氰酸酯基不直接連接到苯環上的芳香族異 〇 驗㈣,本發明提供具有優異加卫性能和低發泡體彈㈣軟質聚氨酿低 回彈發泡體。此外,本發明公開了製備較寬硬度範圍的軟質聚氨醋低回彈 發泡體,而不使用不同於水的其他發泡劑的一步法。 本發明公開了一種新型脂肪族或脂環族或異氰酸酯基不直接連接到笨 %上的芳香族異氰酸酯基聚氨酯材料。本發明聚氨酯材料適合製備軟質聚 氨酯低回彈發泡體,所述軟質聚氨酯低回彈發泡體可用作胸罩墊、肩墊的 材料,還適用於床塾、枕頭、傢倶墊、毯片和汽車坐墊。它特別適用於床 墊和枕頭。 本發明一步法中,將配方材料同時注入混合頭,然後倒入模具内或輸送 ▼上發泡反應進行非常快。根據所用催化劑’上升的發泡體泡沫在 分鐘内基本完全固化^然後使所得發泡體後固化24小時以獲得其最終性能。 本發明方法中,反應組合物包含異氰酸酯组分、異氰酸酯活性組分、催 化Μ、表面活性劑、作為發泡劑的水和本身已知的添加劑。需要的情況下, 還可使用其他添加劑如顏料/染料、抗氧劑、UV吸收劑、阻燃劑、填料、 回收發泡體粉末、穩定劑、抗菌化合物和抗靜電劑。 所述異氰酸酯包括脂肪族和/或脂環族和/或異氰酸酯基不直接連接到苯 %上的芳香族二異氰酸酯單體,或脂肪族和/或脂環族和/或異氰酸酯基不直 14 201037000 接連接到苯環上的芳香族二異氰酸醋單體與三聚體的共混物,所述三聚體 為脂肪族或脂環族或異氰直接連制苯環上的芳軸二異氣酸醋 ' 三聚反應的產物,所述共混物中的NCO含量為20.5-50.0重量份(以異氰酸 . =組分中綱重量份總異氰_計)’計算官能度為2_3。所述脂肪族或^ 環族或異氰酸S旨基;f直接連接到苯環上的芳香族異氰酸醋可為選自但不限 於以下的至少-種:六亞甲基二異氰義、六亞甲基三異氰咖、雙環庚 院三異氰義、十-烧二異氰義、十—烧三異氰_旨、異佛爾嗣二異氛 酸醋、二環己基甲燒二異氰酸醋、甲基環己烧二異氰酸醋、二甲基環己烷 —異氰酸酯、苯二亞甲基二異氰酸S旨、四曱基苯二亞甲基二異紐醋、其 二雜和三聚體。這些異氰㈣巾,制優選六亞曱基二異氰_和異佛 爾酮二異氰酸酯。 、 除了脂肪族和/或脂環族和/或異氰酸醋基不直接連接到苯環上的芳香族 異氰SaJ曰單體和二聚體外’所述異氰酸酿組分任選還包含至多35〇/。重量(以 異氰細旨組分總重計)、包含2-4個異氰酸醋官能围的脂肪族或脂環族或異 氰酸知基不直接連接到苯環上的芳香族異氰酸酯預聚物。 所述異氰酸醋的使用量-般為:異氰酸酷指數為約65_11〇、優選約 _ 70-105、更優選為约75-105。 ❹ 所述異氰酸酯活性混合物包含: (bl)第一異氰酸醋活性組分,所述異氰酸酯活性組分具有至少26個異 氰酸酿活性基、優選為2.6-6.5個異氰酸酿活性基、更優選為2.65_6 〇個異 氰酸醋活絲、最優選為2.7·5.5個異氰_旨活縣,祕當量低於_、 優選為80-800、更優選為100-700、最優選為11〇_6〇〇,羥基值高於7〇吨 KOH/g、優選為 70-700 mg KOH/g、更優選為 8〇_56〇 mg K〇H/g、最優選為 90-510 mg KOH/g, (b2)第一異酸性組分’所述異氰酸自旨活性組分的平均輕基官能度 15 201037000 低於6_0、優選為1.8-6.0、更優選為1.85-4.5,羥基當量為600-6,000、優選 為 700-5,000、更優選為 800-4,500,羥基值為 9-94 mg KOH/g、優選為 19-80 mgKOH/g、更優選為14-70mgKOH/g’第一級羥基含量為至少30重量份、 優選至少40重量份、更優選至少51重量份,以所述第二異氰酸酯活性組 分羥基總重量為100重量份計, 其中所述苐一異氰酸酯活性組分的使用量為20-90重量份,優選20-70 重量份,所述第二異氰酸酯活性組分的使用量為1〇_8〇重量份、優選3〇_8〇 重量份’都以100重量份所述異氰酸酯活性混合物計;和 Ο 任選的重均分子量為60-420g/mol、具有至少兩個異氰酸酯活性官能團 的交聯劑,其中如果使用,所述交聯劑的使用量為〇.2_15重量份、優選0 5_15 重量份、更優選0.5-12重量份、最優選1.2-12重量份,以100重量份所述 異氰酸酿活性混合物計。 任選,所述異氰酸酯活性組分可還包含〇_5〇重量份、優選0-40重量份 (以100重量份異氰酸酯活性組分計)聚合物多元醇,所述聚合物多元醇的固 含量為5_55重量份、更優選10-45重量份(以1〇〇重量份聚合物多元醇計), 羥基值為 15-50mgKOH/g。Another embodiment of the invention relates to a method by employing a body. One-Step Preparation of Soft Polyurethane Low Resilience Foam Another embodiment of the present invention relates to a flexible polyurethane low resilience foam prepared by the above method and having a ruthenium (four) kg/m3. The invention further discloses a method for preparing a tantalum mold "ammonia" foam. = Sending and removing her rebound foam preparation, no special changes are required to the existing negotiable equipment. The isocyanide active composition of the present invention has a large density and hardness range. _ Soft «Ammonia vinegar low back 13 201037000 Elastomeric foam preparation provides a larger range of formulation components. [Embodiment] The present invention relates to a novel soft polyurethane low resilience foam which is obtained by directly isocyanate isocyanate which is substantially free of isocyanate and is directly attached to a benzene ring. The active component and the catalyst, the water, the surface bioassay, the crosslinking agent and the additive are reacted to prepare. The isocyanate red component is selected from one or more of the following isocyanates: aliphatic isocyanates, alicyclic isocyanates, and aromatic isocyanates in which the isocyanate groups are not directly attached to the acyclic ring. When using aliphatic and/or alicyclic and/or isocyanate groups which are not directly bonded to the benzene ring (IV), the present invention provides excellent curing performance and low foaming body bombs. Rebound foam. Further, the present invention discloses a one-step process for preparing a soft polyurethane low resilience foam having a wide hardness range without using other blowing agents other than water. The present invention discloses a novel aliphatic or alicyclic or isocyanate group which is not directly bonded to the aromatic isocyanate-based polyurethane material. The polyurethane material of the invention is suitable for preparing flexible polyurethane low resilience foam, and the soft polyurethane low resilience foam can be used as a material for a bra pad and a shoulder pad, and is also suitable for a mattress, a pillow, a mattress, a carpet sheet. And car seat cushions. It is especially suitable for bed mats and pillows. In the one-step method of the present invention, the formulation material is simultaneously injected into the mixing head, and then poured into the mold or transported to the foaming reaction to proceed very quickly. The foam foam which rises according to the catalyst used was substantially completely cured in a minute, and then the resulting foam was post-cured for 24 hours to obtain its final properties. In the process of the present invention, the reaction composition comprises an isocyanate component, an isocyanate-reactive component, a ruthenium hydride, a surfactant, water as a foaming agent, and an additive known per se. Other additives such as pigments/dyes, antioxidants, UV absorbers, flame retardants, fillers, recycled foam powders, stabilizers, antibacterial compounds, and antistatic agents may also be used as needed. The isocyanates include aliphatic and/or alicyclic and/or isocyanate groups which are not directly bonded to the benzene% aromatic diisocyanate monomer, or aliphatic and/or cycloaliphatic and/or isocyanate groups are not straight 14 201037000 a blend of an aromatic diisocyanate monomer and a trimer attached to a benzene ring, the trimer being an aliphatic or alicyclic or isocyanide directly bonded to the aromatic axis of the benzene ring The product of the homopolymeric acid vinegar 'trimerization reaction, the NCO content in the blend is 20.5-50.0 parts by weight (based on isocyanic acid. = component weight percent total isocyanide), the calculated functionality is 2_3. The aliphatic or cycloaliphatic or isocyanate S group; the aromatic isocyanic acid vine directly attached to the benzene ring may be at least one selected from the group consisting of: hexamethylene diisocyanide Yi, hexamethylene triisocyanate, double-ring Gengyuan triisocyanide, ten-burn diisocyanide, ten-burning tri-iso- cyanide _, different phorrene diiso-sour vinegar, dicyclohexyl Burned diisocyanate, methylcyclohexanyl diisocyanate, dimethylcyclohexane-isocyanate, benzodiamethylene diisocyanate, tetradecylbenzene dimethylene diiso Vinegar, its dimers and trimers. These isocyanate (tetra) towels are preferably hexamethylene diisocyanate and isophorone diisocyanate. In addition to the aliphatic and/or alicyclic and/or isocyanate groups, which are not directly attached to the aromatic isocyanate SaJ on the benzene ring and dimerized in vitro, the isocyanate-stirring component is optionally further Contains up to 35〇/. Weight (based on the total weight of the isocyanide component), an aromatic isocyanate containing 2-4 isocyanate functional groups or an aliphatic or alicyclic or isocyanate group not directly attached to the benzene ring Polymer. The isocyanic acid is used in an amount such that the isocyanic acid has an index of about 65 to about 11 Torr, preferably about _70 to 105, more preferably about 75 to 105. The isocyanate-reactive mixture comprises: (bl) a first isocyanate-reactive component having at least 26 isocyanic acid-reactive groups, preferably from 2.6 to 6.5 isocyanate-stabilizing groups More preferably, it is 2.65_6 异 异 异 异 活 、 live, most preferably 2.7·5.5 isocyanide _ oshi County, the secret equivalent is less than _, preferably 80-800, more preferably 100-700, most preferably 11〇_6〇〇, the hydroxyl value is higher than 7〇KOH/g, preferably 70-700 mg KOH/g, more preferably 8〇_56〇mg K〇H/g, most preferably 90-510 Mg KOH / g, (b2) the first iso-acid component 'the average light-weight functionality of the isocyanic acid-reactive component 15 201037000 is less than 6_0, preferably 1.8-6.0, more preferably 1.85-4.5, The hydroxyl equivalent is from 600 to 6,000, preferably from 700 to 5,000, more preferably from 800 to 4,500, and the hydroxyl value is from 9 to 94 mg KOH/g, preferably from 19 to 80 mgKOH/g, more preferably from 14 to 70 mgKOH/g' The primary hydroxyl group content is at least 30 parts by weight, preferably at least 40 parts by weight, more preferably at least 51 parts by weight, based on 100 parts by weight of the total weight of the second isocyanate active component hydroxyl group, wherein The isocyanate active component is used in an amount of 20 to 90 parts by weight, preferably 20 to 70 parts by weight, and the second isocyanate active component is used in an amount of 1 〇 8 〇 by weight, preferably 3 〇 8 〇. The parts by weight are all based on 100 parts by weight of the isocyanate-reactive mixture; and Ο an optional cross-linking agent having a weight average molecular weight of from 60 to 420 g/mol, having at least two isocyanate-reactive functional groups, wherein if used, the cross-linking The agent is used in an amount of from 2 to 15 parts by weight, preferably from 0 5 to 15 parts by weight, more preferably from 0.5 to 12 parts by weight, most preferably from 1.2 to 12 parts by weight, based on 100 parts by weight of the isocyanuric acid-active mixture. Optionally, the isocyanate-reactive component may further comprise 〇_5 〇 by weight, preferably 0-40 parts by weight (based on 100 parts by weight of the isocyanate active component) of a polymer polyol, the solid content of the polymer polyol It is 5 to 55 parts by weight, more preferably 10 to 45 parts by weight (based on 1 part by weight of the polymer polyol), and has a hydroxyl value of 15 to 50 mgKOH/g.

Q 任選’所述異氰酸酯活性組分可包含0-5.0重量份、優選〇_3.5重量份(以 〇重量伤發泡體總質量計)聚環氧丙烧(b3)作為開孔劑,所述聚環氧丙烧的 名義經基官能度為1,重均分子量為400_9,600 g/md、優選6〇〇 9 〇〇〇 g/m〇l、 更優選 800-8,500 g/moL· 可用於本發明的異氰酸酯活性組分包括大量化合物。它們的良好實例包 括但不傷限於以下:⑷聚鱗多元醇,包括多經基院烴的環氧院烴加成物; 0)聚(四亞曱基醚)二醇和(c)聚(三亞曱基醚)二醇。 上述多羥基烷烴的環氧烷烴加成物實例包括以下物質的環氧烷烴加成 物.乙二醇、二乙二醇、一縮丙二醇、以丙二醇、u_丙二醇、丁二醇、 16 201037000 戍二醇、甘油的三環氧丙烧加成物、三經甲基丙烧單稀丙基鍵、^_三經 甲基乙烧、1,1,1-三赵曱基丙炫、1,2,3-三經曱基己烧、甘油、季戊四醇、聚 - 己内醋、木糖醇、阿拉伯糖醇、山梨醇和甘露醇。使用的環氧烧烴中,最 . 優選環氧乙烧、環氧丙烧和環氧丁炫。 由這種引發娜備的聚⑽多元騎常通過陰離子聚合法製備,其中將環 氧紐與引發劑化合物和驗性催化劑如氫氧化卸或某些有機胺混合。採 用這些強雜雜酿魏驗聚合,會導致補合度提高和所得聚謎多 元醇的平均錢該少。這些不齡組分具杨軌味财延遲多元醇與 0 異氰酸酯反應過程中氨基曱酸乙酯的形成。 雙金屬氰化物(DMC)整合物為取所周知的環氧烧烴聚合催化劑。與採用 強驗性催化㈣備_似多7〇醇相比,這些活性催化劑可祕製備具有極 低不飽和度的聚越多元醇。不飽和組分含量低至〇 〇2咖你的聚_元醇 可採用DMC催化劑製備。基於DMC的聚越多元醇,如2〇〇ι年n月7日 頒布的EP0894108B1中描述的產物,可用於製備氣味減輕、力學性能提古 的軟質聚氨醋低回彈發泡體,因此是本發明中優選的一種聚喊多元醇。呵 實際上’具有活潑氫(通過Zerewitin〇ff(澤爾維季諾夫)測試確定)的任何 〇 材料可用作聚—元醇的組分。例如,贿端的?《多元轉已知的且可 使用。 在本發明中,第-異氰酸_活性組分(bl)必須具備至少26個異氛酸酿 活性基、優選為2.6-6.5個異氰_旨活性基、更優選為2 65.個異氛^ 活性基、最優麟2.7·5.5個錢酸騎錄,以滿足製備低哪發泡 需的交聯度’在此官能基值範圍下,為達所需的反應活性,錄當量: 低於_。太高酿基當量將使多元醇反應活性過低,以致無法^二2 反應性的異氰航反應不翻於本發明。錄當量過低,則無 低回彈發泡體物性所需的適當聚合物分子鏈。優選的經基當量範圍^ 17 201037000 80-800、更優選的羥基當量範圍為1〇〇_7〇〇、最優選的羥基當量範圍為 110-600 〇 本發明賴的帛二異紐騎性齡㈣巾,綠錄絲必須低於 6.0,以達到提供低回彈發泡體物性的需求。過高的官能基數需配合較大的 羥基當量,從而使反應性過低,無法適用於本發明。反之,過低的官能基 數則大幅減損發泡體的物性,特別是拉伸強度及撕裂強度。優選的羥基官 能基數為1.8-6.0、更優選的羥基官能基數為185_4 5。 第二異氰酸S旨活性組分(b2)巾,錄當量舰的細為__6,_、更優 Ο 選的細為.5,_、最優選的範圍為_·4,·。過高醜基當量將造成 反應活性低下,吏不能適用於本發明。太低的經基當量,將使發泡體的 父聯密度過1¾ ’使製得的發雜太硬’並且增加發泡體在溫度變化時相對 硬度的變化。 在第二異氰酸酯活性組分(b2)中,為配合優選的羥基官能基數和經基當 量範圍,必須使用高反應性的第-級織封端的多元醇^為滿足本發明中 與低反應性異氰義製備伽彈發泡_需求,所選㈣第二異氮酸醋活 性組分㈣中必須含有至少3〇重量份、優選至少4〇重量份、更優^少 〇 51重量份的第—級封端,均以所述第二異氰_活性組分㈣的經基 重量計。 可用於本發明的另-類多元醇為上述聚(四亞甲基鍵)二醇。聚㈣亞甲基 喊)二賴四氫领娜)的開環聚合產物。聚(四亞甲蝴二醇為騎多二 醇。它還已知為PTMEG或聚四氫呋鳴和各種商品名如“丁減撕,,和 ‘TdyTHF”。它通過四氫,_催輯合製備。所得聚合物為適當大小, 通常數均分子量為25〇·3,_ g/md。這顿四亞ψ _)二醇巾騎有声某 為第-級經基。本發明中,平均分子量為__3,_、更優選i,孤2二 的聚(四亞甲基醚)二g|為特職選的聚(四亞甲基蜮)二醇。 18 201037000 可用於本發明的第三類多元醇為聚(三亞?二 通過u-丙二醇引發的氧雜環丁_聚 步連續縮聚反應而製備,如2〇〇6 Β Μ 醉)新i夕 7,074,968 = 晖獲侍的丨,3_丙二醇可用作所述生產法中的 進料來製備可再生、可生物轉的聚(三亞f 產去中的 醚)二醇具有第-級經基和低嫁 ▲ — (二亞甲基 必格點及向柔順性。聚(三亞甲基醚 =重均分子量為购,_、_是丨,綱·3,_麵_ 回彈發泡體。採用這種聚(三亞f_)二醇的另—動機來自其可^ Ο 牛雜1 ’仙“賴麵體重量·重量的這些生祕 越)二酵來製備生物可降解的軟質聚氨i旨低回彈發泡體。 „優選用於本發明的多_包括聚(環氧秘·環氧消二醇。當使用時, _乙烧可雜何方式結合到聚合物鏈上。環氧乙斜結合助部鏈段、 作^端鏈段或沿著多元醇鍵隨機分布,選為環氧乙賴端的聚(環氧乙 烧-環氧丙烧)二醇。 交聯丄’且刀可為可011侧或邮基,更具體地脂肪族或脂環族〇H、 NH^或丽2基、重均分子量為4〇_64〇、優選⑼-似咖〇ι、具有至少兩個 〇活性官能_交·,其中如果錢,所述交聯議使用量為 2 15優選0.5-15、更優選〇 5_12、最優選i 2-i2重量份’以1〇〇重量份 所述異氰酸酯活性混合物計。 =聯d的典型實例為:乙二醇、二乙二醇、三乙二醇、四乙二醇、數均 刀^低於_的聚乙二醇、丙二醇、一縮丙二醇、分子量低於的聚 丙一醇丁一一醇、戊二醇、己二醇、三經甲基乙烧、Μ]三經甲基丙 ^、jl2’3_二經曱基己健、甘油、聚(環氧丙烧-環氧乙烧)、聚(環氧丙烧)、 聚(%氧乙烧)、2-甲基_u_丙二醇、3_甲基·戊二醇、Μ.環己二醇、新戊 一SJ、1,4-¼己炫二甲醇、乙二胺、單乙醇胺、二乙醇胺、2_氨基_2·甲基小 丙醇、N_甲基乙_、異佛細二胺和聯胺。所述交聯綱優選實例為單 201037000 乙醇胺和—乙醇胺4果需要’還可制幾種交聯劑的混合物。 —視所述低哪發泡體硬度的f要,在麟異驗騎性混合物中可添加 1、二政的聚合物多㈣。穩定分散的聚合物多元醇組分可為任何聚環氧 烧烴多元醇’具有分散於射的_不飽和單體的聚合彳卜穩定分散的聚 ^物多元醇的典型實例包括聚環氧烧烴多元醇,其中分散有聚(苯乙稀-丙稀 月)矛/或聚脲。所述穩定分散的聚合物多轉可購自幾個公司,包括 。y (,爷耳)(商°°名為Polymer P〇lyol(聚合物多元醇),,)、BASF(巴斯夫X商 名為Graft P〇ly〇i(接枝多凡醇)")、D〇w(商品名為"c叩吻·p〇ly〇1(共聚 Ο物多元醇)")和M0BAY(商品名為',™ PolyoKPHD多元醇),>Bayer、娜 和¥產品中’按照美國專利4,272,619、美國專利4,_,935和美國專利 5,4Η957中所述方法將聚(苯乙稀·丙浠腈)分散於多元醇,定分散的聚合 物多元醇商品的實例列於如下表1 :Q optionally 'the isocyanate-reactive component may comprise 0-5.0 parts by weight, preferably 〇-3.5 parts by weight (based on the total mass of the foam of the ruthenium weight), the polyglycolide (b3) as a cell opener, The polyglycidil has a nominal warp functionality of 1, and a weight average molecular weight of 400_9,600 g/md, preferably 6〇〇9 〇〇〇g/m〇l, more preferably 800-8,500 g/moL· The isocyanate-reactive component of the present invention includes a large amount of a compound. Good examples of these include, but are not limited to, the following: (4) polyquaternary polyols, including epoxy-based hydrocarbon adducts of polyalkylene hydrocarbons; 0) poly(tetradecyl ether) glycol and (c) poly (Sanya Mercapto ether) diol. Examples of the above alkylene oxide adducts of polyhydroxyalkanes include alkylene oxide adducts of the following materials: ethylene glycol, diethylene glycol, propylene glycol, propylene glycol, u-propylene glycol, butylene glycol, 16 201037000 戍Glycol, glycerol, tri-glycidyl-sinter adduct, tri-methyl-propan-single-single-propyl bond, ^_three-methyl-ethyl bromide, 1,1,1-tri-zhao-di-propyl, 1,2, 3-trimethylpyrene, glycerin, pentaerythritol, poly-caprolactone, xylitol, arabitol, sorbitol and mannitol. Among the epoxy burning hydrocarbons used, the most preferred ones are epoxy bake, propylene bromide and butyl bromide. The poly(10) multicapsules from which this is initiated are often prepared by anionic polymerization in which the cyclooxygen is mixed with an initiator compound and an inert catalyst such as a hydroxide or some organic amine. The use of these strong hybrids to test the polymerization will result in an increase in the degree of recombination and an average of less than the average amount of the poly-polyol. These age-old components have the formation of amino decanoate during the reaction of the polyol with the 0-isocyanate. The double metal cyanide (DMC) integrase is a well known epoxy burning hydrocarbon polymerization catalyst. These active catalysts make it possible to prepare poly-polyols with very low unsaturation compared to the use of highly catalyzed (iv)-like 7-merol. The content of unsaturated components is as low as 〇 咖 2 coffee. Your poly-alcohol can be prepared using DMC catalyst. The DMC-based poly-polyol, such as the product described in EP0894108B1 issued on July 7th, can be used to prepare soft polyurethane slow rebound foam with reduced odor and improved mechanical properties. A preferred poly-polyol in the present invention. In fact, any bismuth material with active hydrogen (determined by Zerewitin ff (Zelvidinov) test) can be used as a component of poly-alcohol. For example, bribes? “Multiple turns are known and available. In the present invention, the first isocyanic acid-active component (b1) must have at least 26 octa-acidic active groups, preferably 2.6-6.5 isocyanide-active groups, more preferably 2 65. Efficient ^ Active base, the best 2.7 · 5.5 money acid riding to meet the degree of crosslinking required to prepare low foaming 'In this range of functional values, in order to achieve the required reactivity, recording equivalent: low to_. Too high a base equivalent will make the polyol reactivity too low, so that the isocyanic reaction which cannot be reacted is not turned into the present invention. If the recording equivalent is too low, there is no suitable polymer molecular chain required for low rebound foam physical properties. A preferred base equivalent range is 17 201037000 80-800, a more preferred hydroxyl equivalent range is 1〇〇_7〇〇, and a most preferred hydroxyl equivalent range is 110-600. (4) Towels, the green silk must be less than 6.0 in order to meet the demand for low resilience foam properties. Too high a number of functional groups are required to match a large hydroxyl equivalent, so that the reactivity is too low to be suitable for use in the present invention. Conversely, too low a functional base greatly detracts from the physical properties of the foam, particularly tensile strength and tear strength. A preferred hydroxyl functional group number is from 1.8 to 6.0, and a more preferred number of hydroxyl functional groups is from 185 to 45. The second isocyanic acid S is an active component (b2) towel, and the fineness of the equivalent ship is __6, _, and the fineness of the preferred one is .5, _, and the most preferable range is _·4, ·. Too high a ugly base equivalent will result in a low reactivity and it is not suitable for use in the present invention. Too low a base equivalent will cause the foam to have a parental density of more than 13⁄4' to make the resulting impurities too hard' and to increase the relative hardness of the foam as the temperature changes. In the second isocyanate-reactive component (b2), in order to match the preferred number of hydroxyl functional groups and the base equivalent range, it is necessary to use a highly reactive first-stage woven end-capped polyol to satisfy the low reactivity of the present invention. Cyanide preparation of the gauze foaming_required, the selected (iv) second isocyanate active component (4) must contain at least 3 parts by weight, preferably at least 4 parts by weight, more preferably less than 51 parts by weight of the first - The stage capping is based on the basis weight of the second isocyanate-active component (iv). Another type of polyol which can be used in the present invention is the above poly(tetramethylene bond) diol. Poly(tetra)methylene is a ring-opening polymerization product of shii) tetrahydrotetrahydro). Poly(tetramethylene diol) is a polypoly diol. It is also known as PTMEG or polytetrahydrofuran and various trade names such as "Dings, and 'TdyTHF". It passes tetrahydrogen, _ 催Prepared. The obtained polymer is of a suitable size, usually having a number average molecular weight of 25 〇·3, _ g/md. This quaternary ψ ) 二醇 二醇 骑 骑 骑 骑 某 某 。 。 。 。 。 。 。. In the present invention, the poly(tetramethylene ether) dig| having an average molecular weight of __3, _, more preferably i, or 2 is a special poly(tetramethylene fluorene) diol. 18 201037000 The third type of polyol which can be used in the present invention is prepared by poly (tri-?? di-oxo-polymerization-initiated polycondensation reaction initiated by u-propanediol, such as 2〇〇6 Β 醉 drunk) new i eve 7,074,968 = 获 获 获, 3_ propylene glycol can be used as a feed in the production process to prepare a renewable, bio-transformable poly(tri-f-produced ether) diol with a first-order permeation and a low Marry ▲ — (Dimethylene must be point and compliant. Poly (trimethylene ether = weight average molecular weight for purchase, _, _ is 丨, 纲·3, _ surface _ rebound foam. Use this The other motive of poly(trimide f_) diol is derived from the fact that it can be used to prepare biodegradable soft polyurethane. Elastomeric foam. „Multiple _ preferably used in the present invention include poly(epoxy succinyl epoxide epoxide. When used, _ ethane can be mixed into the polymer chain in any way. The auxiliary part chain, the end chain part or randomly distributed along the polyol bond, selected as the poly(epoxy Ethylene-glycidyl) diol at the epoxy end. The cross-linking 且' 011 side or postal basis, more specifically aliphatic or cycloaliphatic 〇H, NH^ or 丽 2 group, weight average molecular weight of 4〇_64〇, preferably (9)-like ca 〇ι, having at least two 〇 activities Functionality, wherein, if money, the crosslinking agent is used in an amount of 2 15 preferably 0.5-15, more preferably 〇5_12, most preferably i 2-i2 parts by weight 'in terms of 1 part by weight of the isocyanate reactive mixture Typical examples of the combination of = ethylene glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, number average knife ^ lower than _ polyethylene glycol, propylene glycol, propylene glycol, molecular weight is lower than Polypropanol butanol, pentanediol, hexanediol, trimethylacetate, hydrazine] trimethyl propyl hydride, jl2'3 _ dipyridyl hexyl, glycerin, poly (epoxy Propylene-epoxyethane), poly(epoxypropane), poly(% oxyethylene), 2-methyl-u-propylene glycol, 3-methyl-pentanediol, ruthenium hexanediol, Xinyi SJ, 1,4-1⁄4 hexamethylene dimethanol, ethylenediamine, monoethanolamine, diethanolamine, 2-amino-2-methylpropanol, N-methylethyl _, isophora diamine and a hydrazine. A preferred example of the cross-linking unit is a single 201037000 ethanolamine and - Ethanolamine 4 requires a mixture of several crosslinkers. - depending on the hardness of the foam, it can be added to the mixture of the two. The stable dispersed polymer polyol component can be any polyepoxy-fired hydrocarbon polyol. A typical example of a polymerized hydrophobically dispersed polymer polyol having dispersed-infused monomers includes polyepoxy. a hydrocarbon-burning polyol in which poly(styrene-propylene) spears/polyureas are dispersed. The stable dispersed polymer can be purchased from several companies, including .y (, er) °° is called Polymer P〇lyol (polymer polyol),), BASF (BASF X trade name Graft P〇ly〇i (grafted polyol) "), D〇w (trade name &quot ;c叩 kiss·p〇ly〇1 (copolyester polyol)") and M0BAY (trade name ',TM PolyoKPHD polyol), >Bayer, Na and ¥ products in accordance with US Patent 4,272,619, USA The method described in the patents 4, _, 935 and U.S. Patent 5, 4, 957, the dispersion of poly(styrene-propenonitrile) in a polyol, and the dispersion of a polymer polyol. Examples are listed in Table 1 below:

Bayer· "P〇lymer p〇iyol(聚合物多元醇) HS-100 Niax E694 BASF "Graft Polyol(接枝多元醇)„Bayer "P〇lymer p〇iyol (Polymer Polyol) HS-100 Niax E694 BASF "Graft Polyol

Pluracol 1103Pluracol 1103

Voranol 3943 E9232Voranol 3943 E9232

Dow "Copolymer Poly〇l(共聚物多元醇),,Dow "Copolymer Poly〇l (copolymer polyol),

Mobay "PHD Poly〇l(PHD 多元醇)" I述穩定分散的聚元醇可按照〇ertd在“p〇丨__ Hanm〇b-ethane Handbook(聚氨醋手冊),g. 〇e賊 isbn 0-02-948920-2, Hanser Publisher, 1985) 〇 的聚合物M醇製射可使胁何聚魏舰多元醇作為分散體基體。這 種穩定分散的聚合物多元_活性主要取決於這種穩定分散㈣合物多元 醇製備過程中使關基體多元醇的活性。由於本發日种所使师旨肪族和/ 20 201037000 或脂環族和/或異氰酸醋基不直接連接到笨環上的芳香族多異氛麵的活性 較低,優選名義官能度為2.4-6(更優選2.4-5,6,最優選2·4-5.4)、當量為 8〇0-2,_(更優it 8〇(M,_,最優選【,〇_,_)麵、環氧乙烧含量為 4-28(優選4-24)%重量(以基礎多元醇的重量計)的基體多元醇。 視所述低哪發泡雜倾的需要,在所述異_自旨雜混合物令可 添加開孔娜改善所述伽彈發紐敝縮。開孔獅典型實例包括:穩 定分散的聚合解7L醇、環氧乙⑥含量超過鄕重量份的聚(魏乙烧環氧 丙烧)共聚物、重均分子量超過8〇〇的聚(環氧丁烧_環氧丙烧)共聚物、重均 ❹ 分子罝超過600的聚乙二醇、重均分子量超過4〇〇的聚環氧丙;、粒徑小 於150微米的微矽粉(fiimed siHca)、粒徑小於2〇〇微米的聚四氟乙烯樹脂粉 末、脂肪族羧酸及其鹼金屬或鹼土金屬鹽、脂環族羧酸及其鹼金屬或鹼土 金屬鹽、脂肪族烷烴、脂環族烷烴和二甲基矽油。優選開孔劑組分為穩定 分散的聚合物多元醇、環氧乙烷含量超過5〇%重量份的聚(環氧乙烧_環氧丙 烷)共聚物、重均分子量超過800的聚(環氧丁烧_環氧丙烧)共聚物和重均分 子量超過400的聚環氧丙烷。所述優選開孔劑組分的通常使用量為〇.〇5_2〇 重量份、優選0.5-10重量份,以10〇重量份發泡體總質量計。最優選開孔 劑組分為重均分子量超過400的聚環氧丙烷,所述聚環氧丙烷開孔劑的名 ® 義羥基官能度為丨,重均分子量為400-9,600 g/mo卜優選600-9,000 g/mo卜 更優選800-8,500 g/m〇l,所述聚環氧丙烷開孔劑的通常使用量為〇_5 〇重量 份、優選0-3.5重量份(以1〇〇重量份發泡體總質量計”如果需要,還可使 用幾種開孔劑的混合物。 許多聚氨酯催化劑商品可用於製備本發明軟質聚氨酯低回彈發泡體。 催化劑的通常使用量為0.05-2.0 php(每1〇〇重量份多元醇的重量份數)。代 表性催化劑包括:(1)第三級胺如二(2,2,·二甲氨基)乙醚、二(二甲氨基乙基) 醚 ' N-甲基嗎琳(N-methyl morpholine)、N-乙基嗎#(N-ethyl morpholine)、 N,N-二甲基苄胺、n,N-二甲基乙醇胺、ν,Ν,Ν’,Ν,-四甲基_丨,3-丁二胺、五曱 21 201037000 基二亞丙基三胺、三甲胺、三乙胺、三乙醇胺、三亞乙基二胺和氧化咣啶; (2)二氮雙環烯烴’如丨,5_二氮雙環_(4,3,〇)壬烯-5、1,8二氮雙環-(5,4,0)十 一稀-7、 1,8 二氮雙環-(5,3,〇)葵烯-7、1,5 二氮雙環-(5,4,0)十一烯-5、1,4 二氮雙環-(3,3,0)辛烯-4和二氮雙環烯烴的有機鹽如苯酚鹽;(3)強鹼如鹼和 鹼土金屬醇鹽、氫氧化物和酚鹽;(4)強酸的酸性金屬鹽如氣化连錫、氣化 鐵、二氣化錄、氯化叙和;5肖酸鹽;(5)各種金屬的螯合物如採用乙醢丙酮、 本甲醯丙嗣、二氟乙酿丙_、乙酿乙酸乙酯、水楊酿、環戊酿J-2-缓酸酯、 乙醯丙酮亞胺、二乙醯丙酮_亞烷基二亞胺和水楊醛亞胺和各種金屬如鈹、 鎂、鋅、鉛、鈦、锆、錫、鉍、鉬、錳、鐵、鈷和鎳獲得的那些丨⑹各種 金屬的醇鹽和酚鹽如Sn(0R)4、Sn(0R)2、Ti(〇R)4和A1(〇R)3,其中R為烷 基或苯基,和醇鹽與羧酸、二酮和2-(N,N_:烷氨基)烷醇的反應產物, 如通過這樣或類似步驟獲得的鈦螯合物;(7)有機酸與各種金屬如鹼金屬和 鹼土金屬的鹽如己酸鈣、醋酸亞錫、辛酸亞錫和油酸亞錫;(8)四價錫 '三 價和五價砷、銻和鉍的有機金屬衍生物,和鐵和鈷的金屬羰基化合物。 上述催化劑甲,發現有機錫化合物特別可用於製備本發明軟質聚氨酯 低回彈發泡體。優選的有機錫化合物為緩酸的二烧基錫鹽,如二醋酸二丁 基錫、二月桂酸二丁基錫、二月桂酸二甲基錫、馬來酸二丁基錫、二醋酸 -雜祕和二雜二辛絲。其他有时鶴化合物為絲化三烧基 錫、氧化二錫、二絲基二錄錫、二氣化二絲錫和二硫醇二烧二 錫。這些化合物的實例包括氫氧化三甲基錫、氫氧化三丁基錫、氯氧化二 辛基錫、氧化二丁祕、氧化二辛顧、氧化二月桂基錫、二氣二丁基锡、 二氣=辛基錫、二硫醇二丁基錫和二硫醇二甲基錫。所述有機錫化合物的 使用董-般為異氰酸g旨活性混合物(b)的約〇 〇5_約〇 8%重量,優選約〇 Μ 約 0.55°/。重量。 、' ._ 另-可用於本發較《氨s旨低轉魏難财的伽^為布 特(Bronsted)酸與各種驗金屬或驗土金屬的鹽。發現魏氮納或碳酸鱗別 22 201037000 可用於製備本發明軟質聚氨酯低回彈發泡體。所述鹼金屬或鹼土金屬布忍 司特酸鹽的使用量一般為異氰酸酯活性混合物(b)的約0.01-約〇.8〇/0重量, 優選約0.1-約0.6%重量。 一種或多種表面活性劑也可用於發泡組合物。表面活性劑降低本體表 面張力,促進氣泡的成核,使起的泡穩定並使不相容成分乳化。通常用於 聚氨酯發泡體的表面活性劑為聚矽氡院-聚環氧烷烴共聚物,通常使用量為 約0.2-約3%重量、優選約0.6-約2.5%重量,以總異氰酸酯活性混合物計。 用於製備芳香族二異氰酸酯基聚氨酯發泡體的傳統表面活性劑也可用於本 〇 _。 使用0.5-6.5重量份(以100重量份異氰酸酯活性混合物計)水’以通過 與所述異氰酸酯反應產生二氧化碳,作為發泡反應的發泡劑。此外,如果 需要,可使用水和其他已知輔助發泡劑的組合物。特別優選直接使用二氧 化碳(氣體或液體)作為除了水以外的輔助發泡劑。還發現發泡反應過程中調 節氣壓和/或採用機械起泡技術,如1993年12月9日頒布的w〇 93/24304 和1993年3月16日頒布的美國專利5,194,453中所述,可用來改變發泡體 密度。 〇 其他添加劑可任選結合到本發明發泡組合物中。這些其他添加劑包括 但不偈限於.顏料、抗氧化劑、UV吸收劑、UV穩定劑、阻燃劑、填料、 回收發/包aa叙末、穩疋劑、抗微生物化合物和抗靜電劑。這種添加劑不應 對軟質水氣S旨低回彈發泡體的性能有不利影響。 本發明軟質聚氨醋低回彈發泡體可採用模塑法和/或塊料(Slabstock)法 製備。权塑法是其中注入活性混合物,發泡並在密閉模具中模塑的方法。 塊料法是指將活性混合物_在輸送帶上並在開放系統中發泡。 本發明軟質聚氨醋低回彈發泡體密度範圍為約10-約2〇〇公斤/立方公 尺、優選約16'約160公斤/立方公尺,按照瓜K64〇〇方法(溯版)確定。 23 201037000 本發明軟質聚氨酯低回彈發泡體的落球回彈性不高於2〇%、優選不高 於15%,按照JIS K6400方法(1997版)確定。Mobay "PHD Poly〇l(PHD Polyol)" I. Stabilize the dispersed polyhydric alcohol according to 〇ertd in “p〇丨__ Hanm〇b-ethane Handbook, g. 〇e Thief isbn 0-02-948920-2, Hanser Publisher, 1985) The polymer M alcohol shot can be used as a dispersion matrix for this polymer. This stable dispersion of polymer multi-activity depends mainly on The stable dispersion of the (tetra) complex polyol during the preparation of the polyol to activate the base polyol. Due to the present day, the teacher of the aliphatic and / 20 201037000 or alicyclic and / or isocyanate is not directly connected The aromatic polyisotopic surface on the stupid ring is less active, preferably having a nominal functionality of 2.4-6 (more preferably 2.4-5, 6, most preferably 2·4-5.4), and an equivalent weight of 8〇0-2. _ (more preferably it 8 〇 (M, _, most preferably [, 〇 _, _) surface, epoxy Ethylene content of 4-28 (preferably 4-24)% by weight (based on the weight of the base polyol) Matrix polyol. Depending on the need of the low foaming, the heterogeneous mixture may be added to open the pores to improve the camouflage contraction. Typical examples of open-hole lions include: stable dispersion Polymerization solution of 7L alcohol, epoxy E6 content of more than 鄕 parts by weight of poly (Wei E-steam propylene oxide) copolymer, weight average molecular weight of more than 8 〇〇 poly (epoxybutadiene propylene oxide) copolymer , weight average 聚 molecular 罝 more than 600 polyethylene glycol, weight average molecular weight of more than 4 〇〇 polyepoxy; micro-powder powder (fiimed siHca) particle size less than 150 microns, particle size less than 2 〇〇 micron a polytetrafluoroethylene resin powder, an aliphatic carboxylic acid and an alkali metal or alkaline earth metal salt thereof, an alicyclic carboxylic acid and an alkali metal or alkaline earth metal salt thereof, an aliphatic alkane, an alicyclic alkane, and a dimethyl hydrazine oil. The pore component is a stably dispersed polymer polyol, a poly(ethylene oxide-propylene oxide) copolymer having an ethylene oxide content of more than 5% by weight, and a poly(butylene oxide) having a weight average molecular weight of more than 800. a calcined-glycidide copolymer and a polypropylene oxide having a weight average molecular weight of more than 400. The preferred cell opener component is usually used in an amount of 〇5〇2 parts by weight, preferably 0.5-10 parts by weight, to 10 parts by weight of the total mass of the foam. Most preferably, the pore former component is a polypropylene oxide having a weight average molecular weight of more than 400. The name of the polypropylene oxide opener is 丨, the weight average molecular weight is 400-9, 600 g/mo, preferably 600-9,000 g/mo, more preferably 800-8,500 g/m〇, The polypropylene oxide cell opener is usually used in an amount of 〇_5 〇 by weight, preferably 0-3.5 parts by weight (based on 1 gram by weight of the total mass of the foam). If necessary, several openings may be used. Mixture of Agents A number of polyurethane catalyst commercial products are useful in the preparation of the flexible polyurethane low resilience foams of the present invention. The catalyst is usually used in an amount of from 0.05 to 2.0 php (parts by weight per 1 part by weight of the polyol). Representative catalysts include: (1) a tertiary amine such as bis(2,2,dimethylamino)ethyl ether, bis(dimethylaminoethyl)ether N-methyl morpholine, N -ethyl?#(N-ethyl morpholine), N,N-dimethylbenzylamine, n,N-dimethylethanolamine, ν,Ν,Ν',Ν,-tetramethyl-丨, 3-butyl Diamine, quinone 21 201037000 bisdipropylene triamine, trimethylamine, triethylamine, triethanolamine, triethylenediamine and acridine; (2) diazabicycloalkenyls such as hydrazine, 5-diazo Bicyclo-(4,3,〇)decene-5,1,8-diazabicyclo-(5,4,0) eleven-s-7, 1,8-diazabicyclo-(5,3,anthracene) An organic salt of -7,1,5 diazabicyclo-(5,4,0)undecene-5,1,4diazabicyclo-(3,3,0)octene-4 and diazabicycloalkene Phenolate; (3) strong bases such as alkali and alkaline earth metal alkoxides, hydroxides and phenates; (4) acidic acid salts of strong acids such as gasified tin, gasified iron, gasification, chlorination (5) chelates of various metals; such as the use of acetamidine acetone, methacrylate, difluoroethylene, propylene, ethyl acetate, jujube, and glutinous J-2 - retardate, acetamidine Obtained by ketimine, diethyl acetonide _ alkylene diimide and salicylaldimine and various metals such as bismuth, magnesium, zinc, lead, titanium, zirconium, tin, antimony, molybdenum, manganese, iron, cobalt and nickel Those (6) alkoxides and phenates of various metals such as Sn(0R)4, Sn(0R)2, Ti(〇R)4 and A1(〇R)3, wherein R is an alkyl group or a phenyl group, and an alkoxide a reaction product with a carboxylic acid, a diketone and a 2-(N,N-:alkylamino)alkanol, such as a titanium chelate obtained by such or a similar procedure; (7) an organic acid with various metals such as an alkali metal and an alkaline earth metal Salts such as calcium hexanoate, stannous acetate, stannous octoate and stannous oleate; (8) tetravalent tin 'organic metal derivatives of trivalent and pentavalent arsenic, antimony and bismuth, and metal carbonyls of iron and cobalt Compound. The above catalyst A was found to be particularly useful for the preparation of the flexible polyurethane low resilience foam of the present invention. Preferred organotin compounds are diacids of dialkyltin, such as dibutyltin diacetate, dibutyltin dilaurate, dimethyltin dilaurate, dibutyltin maleate, diacetic acid-hetero and diammonium. Xin Si. Other sometimes, the crane compound is a silky tris-based tin, a di tin oxide, a di-silica di-n- tin, a di-vaporized two-filament tin, and a dithiol di-tin-tin. Examples of such compounds include trimethyltin hydroxide, tributyltin hydroxide, dioctyltin oxychloride, dibutyl sulphide, dioxacin oxide, dilauryl tin oxide, dibutyltin dihydrate, dioxane = octyl Tin, dibutyltin dithiolate and dimethyltin dithiolate. The use of the organotin compound is generally about 5% by weight of the active mixture (b) of the isocyanate group, preferably about 0.55 °/. weight. , ' ._ Another - can be used in this issue compared to "Ammonia s low to turn Wei Weicai gamma ^ is a Bronsted acid and various metal or soil test metal salts. It was found that WeiNA or carbonate scales 22 201037000 can be used to prepare the flexible polyurethane low resilience foam of the present invention. The alkali metal or alkaline earth metal benzoate salt is generally used in an amount of from about 0.01 to about 8% by weight of the isocyanate-reactive mixture (b), preferably from about 0.1 to about 0.6% by weight. One or more surfactants can also be used in the foaming composition. The surfactant reduces the surface tension of the body, promotes nucleation of the bubbles, stabilizes the foam and emulsifies the incompatible components. The surfactant commonly used in polyurethane foams is a polyphthalocene-polyalkylene oxide copolymer, usually used in an amount of from about 0.2 to about 3% by weight, preferably from about 0.6 to about 2.5% by weight, based on the total isocyanate reactive mixture. meter. Conventional surfactants for the preparation of aromatic diisocyanate-based polyurethane foams can also be used in the present invention. 0.5 to 6.5 parts by weight (based on 100 parts by weight of the isocyanate reactive mixture) of water is used to generate carbon dioxide by reaction with the isocyanate as a foaming agent for the foaming reaction. In addition, a combination of water and other known auxiliary blowing agents can be used if desired. It is particularly preferable to directly use carbon dioxide (gas or liquid) as an auxiliary blowing agent other than water. It is also found that the gas pressure is adjusted during the foaming reaction and/or the mechanical foaming technique is used, as described in US Pat. No. 5,194,453, issued on Dec. 9, 1993, and U.S. Patent No. 5,194,453, issued on Mar. Change the foam density. 〇 Other additives may optionally be incorporated into the foaming compositions of the present invention. These other additives include, but are not limited to, pigments, antioxidants, UV absorbers, UV stabilizers, flame retardants, fillers, recycled hair/bags, stabilizers, antimicrobial compounds, and antistatic agents. Such an additive should not adversely affect the performance of the soft water vapor S low resilience foam. The soft polyurethane low resilience foam of the present invention can be prepared by a molding method and/or a slabstock method. The plastic molding method is a method in which an active mixture is injected, foamed, and molded in a closed mold. The block method means that the active mixture is foamed on a conveyor belt and in an open system. The soft polyurethane low resilience foam of the present invention has a density ranging from about 10 to about 2 〇〇 kg/m ^ 3 , preferably about 16 ′ to about 160 kg / m ^ 3 , according to the method of melon K64 ( (proofing) determine. 23 201037000 The soft polyurethane low resilience foam of the present invention has a falling ball resilience of not more than 2% by weight, preferably not more than 15%, determined according to the JIS K6400 method (1997 edition).

本發明軟質聚氨自旨伽彈發泡體具有本領域情於軟㈣氨泡體 所理解的硬度。在-個實施方案中,本發明軟f聚氨s旨低回彈發泡體的硬 度小於15GN/314em2。在另-個實财案巾,本發明㈣聚氨雜回彈發 泡體的硬麟6·12_31杨2或者6姻/314em2。核锻f聚氨醋低回 彈發泡體的硬度可通過調整第-異氰酸g旨活性組分⑽和第二異氰酸醋活 性組分(b2)間的比例’和選用適當的異氰酸醋指數而加以調整。使用較多的 第二異誠6旨雜組分〇2)配合不高於8〇的異紐締數,本發明的軟質 聚氨酯低回彈發泡體的IFD25%硬度可調低至6N/314cm2。使用較多的第一 異氰酸酯活性組分(bl)配合不低於95的異氰酸酯指數,本發明的軟質聚氨 醋低回彈發泡體的IFD25%硬度可調高至i2〇N/3l4cm2。IFD25%硬度的測 定依據JISK6400方法(1997版)確定。一般而言,枕頭及床墊用的軟質聚氨 酯低回彈發泡體要求IFD25%硬度介於i2N/314cm2到24N/314cm2之間, 以兼顧承載力及舒適性。運動墊或頭盔等用途則要求高硬度,以達到吸震、 抗衝擊的效果。 具體實施方式The soft polyurethane self-propelled gauze foam of the present invention has a hardness as understood in the art of soft (tetra) ammonia bubble. In one embodiment, the soft f-ammonia s of the present invention has a low resilience foam having a hardness of less than 15 GN/314em2. In another-real financial case, the present invention (4) is a hard-brown rebounding body of hard lining 6·12_31 yang 2 or 6 marital/314em2. The hardness of the nuclear forged f polyurethane low resilience foam can be adjusted by adjusting the ratio between the active component (10) of the isocyanate g and the active component (b2) of the second isocyanate. Adjusted by cyanate vinegar index. Using a second amount of the second heterogeneous 6-components 2) with a different amount of no-bonds of not more than 8 ,, the flexible polyurethane low resilience foam of the present invention can be adjusted to an IFD 25% hardness as low as 6 N/314 cm 2 . . The IFC 25% hardness of the soft polyurethane low resilience foam of the present invention can be adjusted up to i2 〇 N / 3 14 cm 2 using a larger amount of the first isocyanate active component (bl) in combination with an isocyanate index of not less than 95. The IFD 25% hardness was determined according to the JISK6400 method (1997 edition). In general, soft polyurethane low resilience foams for pillows and mattresses require an IFD 25% hardness between i2N/314cm2 and 24N/314cm2 for both load bearing and comfort. For applications such as sports mats or helmets, high hardness is required to achieve shock absorption and impact resistance. detailed description

以下詳細說明中,使用的符號、術語和縮寫將具有以下定義: ISO 1是異佛爾晒一異乳酸醋’產自BayerAG(拜耳)的DesmodurI商品。 ISO 2是50%重置異佛爾_二異氰酸g旨(Desmodur I)和50%重量六亞甲 基二異氰酸酯三聚體(Desmodur N3600商品)的混合物,兩者都產自Bayer AG(拜耳)。 ISO 3是曱苯二異氰酸S旨’為80%重量2,4-甲苯二異氰酸S旨和20%重量 2,6-甲苯二異氰酸酯的組合物’產自BayerAG(拜耳)。 24 201037000 ISO 4是六亞甲基二異氰酸酯,產自Bayer AG(拜耳)的Desmodur Η商 品。 ISO 5是六亞甲基二異氰酸酯經三聚化反應所製備的六亞曱基二異氰 酸醋三聚體’產自BayerAG(拜耳)的DesmocjurN3600商品。 ISO 6是苯二亞甲基二異氰酸酯,產自Mitsui_Takeda Chemicals Inc (三 井-武田化學)的Takenate 5〇0商品。 P 1是甘油引發的聚環氧丙烷,平均分子量為550g/mo卜羥基值為310 mg KOH/g ’ 產自 SK Chemicals of Korea(韓國 SK 化工)的 YUKOL 1030。 〇 P2是山梨醇引發的聚環氧丙烷,平均羥基當量為約1Π。 P 3是聚(四亞曱基輕)二醇,羥基當量為約9〇〇,產自台灣大連化學公 司。 P 4是由生物基1,3-丙二醇製備的聚(三亞甲基醚)二醇,平均羥基當量 為約1,〇7〇,APHA色度大約25,產自丑丄如卩⑽(杜邦)。 P 5是低不飽和度聚醚多元醇,通過採用DMC催化劑使環氧丙烷加成 聚合到一縮丙二醇引發劑,然後用環氧乙烷封端而製備,平均分子量為 © 4,0008/〇1〇卜羥基值為約28«1§哭〇11^,名義官能度為2,第一級羥基官能 團含量為總羥基重量的約87〇/。重量,售自Bayer AG(拜耳)的acclaim POLYOL 4220N。 P 6是低不飽和度聚醚多元醇,通過採用1)1^(:催化劑使環氧丙烷加成 聚合到一縮丙二醇引發劑而製備,平均分子量為4,〇〇〇 g/mo】,羥基值為約 28mgKOH/g,不飽和度為〇_〇〇5meq/g,1〇〇0/〇重量第二級羥基(卿_町 hydroxy,亦稱為仲羥基)官能團,名義官能度為2,售自Bayer AG(拜耳) 的 ACCLAIM POLYOL 4220。 P 7是低不飽和度聚醚多元醇,通過採用DMC催化劑使環氧丙烷加成 25 201037000 聚合到1,1,1-三羥曱基丙烷引發劑而製備,平均分子量為3,000g/m〇l,經基 值為約57.6mgKOH/g,不飽和度為0.005meq/g ’ 100%重量第二級經基官 能團,名義官能度為3,售自BayerAG(拜耳)的ACCLAIMPOLYOL3300N。 , p 8是低不飽和度聚醚多元醇,通過採用DMC催化劑使環氧丙烷加成 聚合到一縮丙二醇引發劑,然後用環氧乙烷封端而製備,平均分子量為 2,000咖〇卜羥基值為約5611^〇啡,名義官能度為2,第一級羥基官能 團含量為總羥基重量的約87%重量,售自Bayer AG(拜耳)的ACCLAIM POLYOL 2220N。 Ο P 9是低不飽和度聚醚多元醇,通過採用DMC催化劑使環氧丙烷加成 聚合到一縮丙二醇引發劑而製備,平均分子量為8,〇〇〇 g/md,羥基值為約 14mgKOH/g’ 100%重量第二級羥基官能團,名義官能度為2,售自Bayer AG(拜耳)的 ACCLAIM POLYOL 8200。 P 10疋聚(環氧丙烷-環氧乙院)共聚物’通過採用氫氧化鉀催化劑使環 氧丙烷加成聚合到一縮丙二醇引發劑,然後用環氧乙烷封端而製備,環氧 乙烧含量為19%重量’第一級羥基官能團含量為總羥基重量的約53。/〇重 ΐ ’平均分子量為2,000 g/mo卜經基值為約56J mg K〇H/g,不飽和度為 ❹ 0.03 meq/g,名義官能度為2。 泛(衣我丙烧"'環氧乙燒)共聚物’通過採用氫氧化卸催化劑使環 =丙院加成4合到山梨醇引發劑,雌用環氡乙炫封端而製備,環氧乙烧 含置為28%重量,第一級經基官能團含量為總經基重量的約·重量經 基值為約31.3mgKOH/g,名義官能度為6。 /12疋聚。物?謂,分散有俄重量苯乙烯丙烯腈共雜,經基值 為勺28_5 mg ΚΟΗ/g。基财元醇鱗機進料的聚(環氧硫_環氧乙勒三 醇’經基當量為1 〇50,隹& r> ’ σ 自 Bayer AG(拜耳)的 ARCOL POLYOL HS-100。 &疋醇’通過採用氫氧化鉀催化劑使環氧丙烧加成聚合到丁醇 26 201037000 引發劑,羥基值為8.5 mg KOH/g。 DEOA疋—乙醇胺’純度超過99%重量,售自Sigma_Aldrieh(西格瑪奥 德里奇)。 、 PEG 4〇0為試劑級聚(乙二醇),平均分子量為働,純度超過98 5%, 售自Sigma-Aldrich(西格瑪奥德里奇)。 甘油為純度超過99%的GC試劑級甘油,售自別轉-偷此(西格瑪奥 德里奇)。 SC為奴酸鈉# 2M水溶液,由去離子水和純度超過99%賴劑級碳酸 鈉製備’售自Sigma-Aldrich(西格瑪奥德里奇)。 SBC為碳酸氫鈉的0.5M水溶液,由去離子水和純度超過娜的試劑級 破酸氫鈉製備,售自Sigma-Aldrich(西格瑪奥德里奇)。 DC 5950為氧院·聚共聚物表面活性劑,售自Ak pr〇ducts and Chemicals Inc·(空氣化工產品有限公司)的DABC〇DC 595〇。 DC 5179為低釋放型聚石夕氧烧-聚環氧烷烴共聚物表面活性劑,售自他 Products and Chemicals Inc.(空氣化工產品有限公司)的 DABC〇 DC 5179。In the following detailed description, the symbols, terms and abbreviations used will have the following definitions: ISO 1 is a different lactic acid vinegar from the Bayer AG (Bayer). ISO 2 is a 50% replacement of a mixture of Desmodur I and 50% by weight of hexamethylene diisocyanate trimer (Desmodur N3600 commercial product), both from Bayer AG ( Bayer). ISO 3 is a composition of phthalic acid disulfide S which is 80% by weight of 2,4-toluene diisocyanate S and 20% by weight of 2,6-toluene diisocyanate' from Bayer AG (Bayer). 24 201037000 ISO 4 is hexamethylene diisocyanate, a product of Desmodur® from Bayer AG (Bayer). ISO 5 is a hexamethylene diisocyanate trimer prepared by trimerization of hexamethylene diisocyanate. Desmocjur N3600 from Bayer AG (Bayer). ISO 6 is benzene dimethylene diisocyanate, available from Takesu 5: 0 of Mitsui_Takeda Chemicals Inc. P 1 is a glycerin-initiated polypropylene oxide having an average molecular weight of 550 g/mo and a hydroxyl value of 310 mg KOH/g 'YUKOL 1030 from SK Chemicals of Korea. 〇 P2 is a sorbitol-initiated polypropylene oxide having an average hydroxyl equivalent of about 1 Torr. P 3 is a poly(tetrakisinyl) light diol having a hydroxyl equivalent of about 9 Å, which is produced by Dalian Chemical Company of Taiwan. P 4 is a poly(trimethylene ether) glycol prepared from bio-based 1,3-propanediol having an average hydroxyl equivalent of about 1, 〇7〇, and an APHA color of about 25, which is produced from ugly such as ruthenium (10) (DuPont). . P 5 is a low unsaturation polyether polyol prepared by addition polymerization of propylene oxide to a propylene glycol initiator using a DMC catalyst, followed by capping with ethylene oxide, and an average molecular weight of 4,000 8 / 〇 1 〇 hydroxy value is about 28 «1 § crying 11 ^, the nominal functionality is 2, the first-level hydroxyl functional group content is about 87 〇 / of the total hydroxyl weight. Weight, sold by Bayer AG, acclaim POLYOL 4220N. P 6 is a low-unsaturation polyether polyol prepared by using 1) 1 : (: catalyst to propylene oxide addition polymerization to a propylene glycol initiator, the average molecular weight is 4, 〇〇〇 g / mo), The hydroxyl value is about 28 mgKOH/g, the degree of unsaturation is 〇_〇〇5meq/g, and the weight of the second-order hydroxyl group (also known as secondary hydroxyl) is 1〇〇0/〇, and the nominal functionality is 2 , sold by Bayer AG, ACCLAIM POLYOL 4220. P 7 is a low unsaturation polyether polyol, which is polymerized to 1,1,1-trihydroxydecylpropane by using a DMC catalyst to convert propylene oxide to 25 201037000. Prepared with an initiator having an average molecular weight of 3,000 g/m〇1, a base value of about 57.6 mgKOH/g, an unsaturation of 0.005 meq/g '100% by weight of a second-stage hydrocarbyl functional group, and a nominal functionality of 3, ACCLAIMPOLYOL 3300N from Bayer AG (Bayer). p 8 is a low unsaturation polyether polyol prepared by the addition polymerization of propylene oxide to a propylene glycol initiator using a DMC catalyst, followed by capping with ethylene oxide. , the average molecular weight is 2,000, the hydroxyl value is about 5611 ^ morphine, the nominal functionality is 2, the first The primary hydroxyl functional group content is about 87% by weight based on the total hydroxyl weight, sold by ACCLAIM POLYOL 2220N from Bayer AG (Bayer). Ο P 9 is a low unsaturation polyether polyol which is polymerized by propylene oxide using a DMC catalyst. Prepared to a propylene glycol initiator with an average molecular weight of 8, 〇〇〇g/md, a hydroxyl value of about 14 mg KOH/g' 100% by weight of a second-level hydroxyl functional group, a nominal functionality of 2, sold by Bayer AG (Bayer) ACCLAIM POLYOL 8200. P 10 疋 poly(propylene oxide-epoxyether) copolymer 'additional polymerization of propylene oxide to a propylene glycol initiator by using a potassium hydroxide catalyst, and then sealed with ethylene oxide Prepared at the end, the content of the ethylene oxide was 19% by weight. The content of the first-stage hydroxyl functional group was about 53% by weight of the total hydroxyl group. The average molecular weight was 2,000 g/mo. The base value was about 56 J mg K〇H/ g, the degree of unsaturation is ❹ 0.03 meq/g, and the nominal functionality is 2. 泛(衣我丙烧" 'epoxyethyl bromide copolymer' by using a hydrogenation catalyst to reduce the ring = propyl addition 4 To sorbitol initiator, prepared by female ring 氡 炫 封 ,, epoxy B The content is set to 28% by weight, the first-stage trans-functional group content is about 31.3 mg KOH/g of the total weight of the base, and the nominal functionality is 6. 12 疋. Russian weight styrene acrylonitrile co-doped, the base value is 28_5 mg ΚΟΗ / g. The poly(epoxysulfo-epoxytriol) having a base equivalent of 1 〇50, 隹&r> 'σ from Bayer AG's ARCOL POLYOL HS-100. & sterol' by the use of a potassium hydroxide catalyst to add propylene oxide to the butanol 26 201037000 initiator with a hydroxyl value of 8.5 mg KOH / g. DEOA 疋 - ethanolamine 'purity more than 99% by weight, sold in Sigma_Aldrieh (Sigma Aldrich). PEG 4〇0 is a reagent grade poly(ethylene glycol) with an average molecular weight of 働, purity over 98 5%, sold by Sigma-Aldrich (Sigma Aldrich). Glycerin is more than 99 % GC reagent grade glycerol, sold from the other - steal this (Sigma Aldrich). SC is sodium sulphate # 2M aqueous solution, prepared from deionized water and more than 99% pure grade sodium carbonate 'sold from Sigma- Aldrich (Sigma Aldrich) SBC is a 0.5 M aqueous solution of sodium bicarbonate prepared from deionized water and reagent grade sodium hydrogen sulphate of purity over Na, sold from Sigma-Aldrich (Sigma Aldrich). Oxygen and Polycopolymer Surfactant, available from Ak pr〇ducts and Chemicals Inc. (Air Products) DABC〇DC 595〇. DC 5179 is a low release polyoxo-polyalkylene oxide copolymer surfactant sold by his Products and Chemicals Inc. ) DABC 〇 DC 5179.

Niax A-230為第二級胺混合物,售自chemtura Corp.(科聚亞化工有限 公司)。 S〇是指辛酸亞錫,售自Air Products and Chemicals Inc.(空氣化工產品 有限公司)的DABCO T-9。 DBTDL 疋指一月桂酸二丁基錫,售自 Air Products and Chemicals Inc.(空氣化工產品有限公司)的Dabc〇T-12。 UV是2-(2’-羥基-3’5,-二叔戊基苯基)苯并三唑,化學文摘編號為 25973-55-1,由台灣永光化學工業股份有限公司產製。 27 201037000 “指數”是指反應混合物中活性異氰酸酯基的總莫耳數除以反應混合物 中異氰酸酯活性基的總莫耳數之比乘以100。 “pbw”是指重量份。 ' 以下詳細說明中,實施例中給出的聚氨酯發泡體性能按照以下測試方 法確定: “中心密度”按照JIS K6400方法(1997版)確定。 “IFD(Indentation Force Deflection,壓陷力變形)硬度 25%” ’ 是指按照 JISK64〇0方法(1997版)採用25%壓縮負荷確定。 〇 “CLD(Compression Load Deflection,壓縮受力變形)硬度 25%’’,是指按 照JIS K6400方法(1997版)採用25%壓縮負荷確定。 “硬度變化”是指在23°C測定的CLD硬度對照,在-5°C測定的CLD硬 度的提高比例(以%表示)。CLD硬度25%按照JIS K6400方法(1997版)碟 定。測試樣品在測試前在指定溫度下調節至少24小時。 “拉伸強度”按照JIS K6400方法(1997版)確定。 “伸長”按照JIS K6400方法(1997版)確定。 “撕裂強度”按照JIS K6400方法(1997版)確定。 中心的“落球回彈性”按照JISK6400方法(1997版)確定。 按照JIS K6400方法(1997版)確定。 “乾壓縮變形”是指按照JIS K6400方法(1997版)確定的乾熱壓縮變形》 “濕壓縮變形”是指按照JIS K6400方法(1997版)確定的濕熱壓縮變形。 “UV穩定性”值是按照AATCC 16-1990,選項E方法獲得的色牢度測 量。將發泡體樣品放在UV燈下並暴露於紫外光20小時。與標準灰度卡對 28 201037000 比,結果表示為I·5的等級。等級5是指根本沒有顏色變化,等級1是指 幾乎為深色。等級4及以上的值表明沒有裸眼可辨別的目視變化。疋曰 “模壓加讀,,是麵評估,發泡後具餅喊層蝴_發泡體評定 為“良好”,發泡後發泡體收縮但滾軋兩次後恢復的那種評定為“可礙札,,,發 泡後發泡體收縮且滾軋兩次後不恢復的那種評定為“差,,。 以下實施烟來制本發明,科應简如任何方式縣發明範圍 進行任何限定。除㈣有,财份和百分㈣重量份和重量百分比。 實施例1-30和對比f偷例C1-C5 實施例1-10和對比實施例C1-C5 通過將表2-1 #口 2-2中所示的組份混合製備實施例㈣和對比實施例 d-C5的軟質聚細低轉發顏。發泡之前,闕定⑽該分在溫度 控制在23抑的恒溫箱内調節至少24小時。加入有機錫化合物之前,在 1.5升不錄鋼杯内採用旋轉速度設定為^鄉物的c〇wles型混合器在4〇 秒内將除了有機錫化合物和異氰酸醋外的成分預混在一起。預混合後,接 著將有機錫化合物(如果使用)加入杯中,再混合2〇秒,旋轉速度設定為 l,500rpm。然後將選定異氰酸醋化合物加入所得混合物並以3娜哪與所 得組合物混合5秒。織瓶合物倒人頂糾了開的45公分(長)χ45公分 (見)Χ45公分(面)紙襯木盒並發泡。泡洙達到其最終高度後,讓之在盒中靜 置另外十i鐘’然後從盒巾移出來。然後將所製發泡體保存在通風且溫度 控制在27±2°C的儲存室内至少72小時。 然後根據JIS K6400方法(1997版)中描述的樣品尺寸,採用實驗室規模 電動錯機從所製發泡體中心切割出樣品。接著根據ns κ64〇〇方法〇997版) 中描述的樣品尺寸’從指定厚度的發泡體板模切出用於測試撕裂強度、拉 伸強度和伸長的樣品。在物理性能測試之前,使所有樣品在溫度控制在 23±1 C、濕度為50%的恆溫恆濕箱内調節至少24小時。 29 4201037000 表2-1 發泡體算級60kg/m3 實施例 1 配方: P1 (pbw) - 48 P 2 (pbw) 30 — P 5 (pbw) 60 — P 6 (pbw) - — P 7 (pbw) - — P 8 (pbw) - — P 9 (pbw) - — P 10 (pbw) - 50 P 11 (pbw) - — 〇 P 12 (pbw) 6 - P 13 (pbw) - 3 水(pbw) 0.67 0.51 PEG 400 (pbw) 4 2 DEOA(pbw) 1.3 1.1 ISO 1 指數 -- - ISO 2 指數 85 90 ISO 3 指數 一 -- ISO4 指數 -- -Niax A-230 is a second-grade amine mixture sold by Chemtura Corp. S〇 refers to stannous octoate, sold by Air Products and Chemicals Inc. (DACCO T-9). DBTDL refers to dibutyltin monolaurate sold by Dabc(R) T-12 from Air Products and Chemicals Inc. (Air Products). UV is 2-(2'-hydroxy-3'5,-di-tert-amylphenyl)benzotriazole, Chemical Abstract No. 25973-55-1, manufactured by Taiwan Yongguang Chemical Industry Co., Ltd. 27 201037000 "Index" means the ratio of the total number of moles of reactive isocyanate groups in the reaction mixture divided by the total number of moles of isocyanate reactive groups in the reaction mixture multiplied by 100. "pbw" means parts by weight. In the following detailed description, the properties of the polyurethane foams given in the examples were determined according to the following test methods: "Center density" was determined in accordance with JIS K6400 method (1997 edition). "IFD (Indentation Force Deflection) hardness 25%" is determined by a 25% compression load according to the JISK64〇0 method (1997 edition). 〇 “CLD (Compression Load Deflection) hardness 25%” is determined by 25% compression load according to JIS K6400 method (1997 edition). “Hardness change” refers to CLD hardness measured at 23 °C. Control, the ratio of increase in CLD hardness (expressed in %) measured at -5 ° C. The CLD hardness of 25% was determined according to the JIS K6400 method (1997 edition). The test sample was conditioned at the specified temperature for at least 24 hours before the test. Tensile strength" is determined in accordance with JIS K6400 method (1997 edition). "Elongation" is determined in accordance with JIS K6400 method (1997 edition). "Tear strength" is determined in accordance with JIS K6400 method (1997 edition). The center "falling ball resilience" is in accordance with The JISK6400 method (1997 edition) is determined. It is determined according to the JIS K6400 method (1997 edition). "Dry compression deformation" refers to the dry heat compression deformation determined according to the JIS K6400 method (1997 edition) "wet compression deformation" means according to JIS K6400 The wet heat compression set determined by the method (1997 edition). The "UV stability" value is the color fastness measurement obtained according to AATCC 16-1990, Option E. The foam sample is placed under a UV lamp and exposed to ultraviolet light 20 Hour. With standard gray The ratio of the card to the ratio of 28 201037000 is expressed as the level of I·5. The level 5 means that there is no color change at all, the level 1 means almost dark color, and the value of level 4 and above indicates that there is no visual change that can be discerned by the naked eye.曰 "Molding plus reading, is a face evaluation, with a cake layered after foaming _ foam is rated as "good", the foam shrinks after foaming but the recovery after rolling twice is "may In the case of the trouble, the evaluation that the foam shrinks after foaming and does not recover after rolling twice is "poor,". The present invention is embodied in the following embodiments, and the invention should be limited in any way to the scope of the invention. In addition to (d), the amount of money and percentage (four) parts by weight and weight percentage. Examples 1-30 and Comparative Example C1 - C5 Examples 1-10 and Comparative Examples C1 - C5 Examples (4) and comparative examples were prepared by mixing the components shown in Table 2-1 #口2-2. Example d-C5 soft poly-low forwarding face. Prior to foaming, the fraction (10) is adjusted for at least 24 hours in an incubator with a temperature control of 23. Prior to the addition of the organotin compound, the c〇wles type mixer with a rotational speed set to a non-recorded steel cup was premixed with the ingredients other than the organotin compound and isocyanuric acid in 4 seconds. . After premixing, the organotin compound (if used) is then added to the cup and mixed for another 2 seconds, the rotational speed being set to 1,500 rpm. The selected isocyanate compound was then added to the resulting mixture and mixed with the resulting composition for 5 seconds. The weaving bottle is inverted and the 45 cm (length) χ 45 cm (see) Χ 45 cm (face) paper lining wooden box and foaming. After the bubble reaches its final height, let it rest for another ten minutes in the box and then remove it from the towel. The resulting foam was then stored in a ventilated and temperature controlled storage room at 27 ± 2 ° C for at least 72 hours. Then, according to the sample size described in the JIS K6400 method (1997 edition), a sample was cut from the center of the produced foam using a laboratory-scale electric error machine. The sample for testing the tear strength, tensile strength and elongation was then cut from the foam sheet of the specified thickness according to the sample size described in the ns κ 64 〇〇 method 〇 997 version). All samples were conditioned for at least 24 hours in a constant temperature humid chamber with a temperature control of 23 ± 1 C and a humidity of 50% prior to physical performance testing. 29 4201037000 Table 2-1 Foam calculation level 60kg/m3 Example 1 Formulation: P1 (pbw) - 48 P 2 (pbw) 30 — P 5 (pbw) 60 — P 6 (pbw) - — P 7 (pbw ) - P 8 (pbw) - P 9 (pbw) - P 10 (pbw) - 50 P 11 (pbw) - — 〇P 12 (pbw) 6 - P 13 (pbw) - 3 water (pbw) 0.67 0.51 PEG 400 (pbw) 4 2 DEOA(pbw) 1.3 1.1 ISO 1 index --- ISO 2 index 85 90 ISO 3 index one -- ISO4 index ---

Niax A-230 (pbw)— — SC (pbw) 0.8 1.0 DBTDL (pbw) 0.48 0.36 SO (pbw) ~ — -- DC 5950 (pbw) 0.7 0.85 w 發泡體性能: 40i58 9 3 °· 2 5 9 6 3 °· 5 8 °· 40 — 40 40 40 40 50 — 36 — — -- — — — 62 54 — -- — — 58 — :: 57 — :: - __ __ __ 55 — — — 4 — — 60 50 3 3 _ 1.5 1.5 0.39 0.51 0.51 0.68 0.68 0.51 0.51 2 2 2 3 5 — ~ 1.5 1.35 1.5 1.2 1.2 — — 105 — — — — — — — 90 90 — — 95 90 — — — 95 95 — ~ 1.15 1.0 1.0 0.8 0.8 1.0 1.0 0.31 0.31 0.45 0.54 0.57 0.32 0.36 0.85 0.85 0.85 0.7 0.85 0.8 0.8 OK OK OK OK OK OK OK 64.9 59.7 60.6 67.1 69.2 56.3 59.8 42 48 67 32 29 33 31 0.113 0.139 0.198 未測 未測 未測 未測 5.8 18.7 5.3 未測 未測 未測 未測 186 127 134 213 197 171 162 274 248 238 315 302 216 237 191 176 161 196 181 177 182 5 3 3 8 10 4 2 3.1 4.1 3.4 4.7 5.2 7.3 8.6 目視 OK OK 中心密度(kg/m3) 68.2 61.3 IFD 25% (N/314cm2) 87 58 CLD25%硬度 (N/cm2) 0.257 0.156 硬度變化(%) 22.3 7.2 拉伸強度(kPa) 86 166 伸長(%) 164 227 撕裂強度(N/m) 131 152 中心的落球回彈性 (%) 4 4 乾壓縮變形(%) 9.2 4.4 30 201037000 濕壓縮變形(%) 8.8 4.6 3.4 2.6 5 4.5 未測未測未測未測 表2-2Niax A-230 (pbw) — — ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( ( 6 3 °· 5 8 °· 40 — 40 40 40 40 50 — 36 — — — — — — 62 54 — -- — — 58 — :: 57 — :: - __ __ __ 55 — — — 4 — — 60 50 3 3 _ 1.5 1.5 0.39 0.51 0.51 0.68 0.68 0.51 0.51 2 2 2 3 5 — ~ 1.5 1.35 1.5 1.2 1.2 — — 105 — — — — — — — 90 90 — — 95 90 — — — 95 95 — ~ 1.15 1.0 1.0 0.8 0.8 1.0 1.0 0.31 0.31 0.45 0.54 0.57 0.32 0.36 0.85 0.85 0.85 0.7 0.85 0.8 0.8 OK OK OK OK OK OK 64.9 59.7 60.6 67.1 69.2 56.3 59.8 42 48 67 32 29 33 31 0.113 0.139 0.198 Untested and untested Not tested 5.8 18.7 5.3 Untested Untested Untested 186 127 134 213 197 171 162 274 248 238 315 302 216 237 191 176 161 196 181 177 182 5 3 3 8 10 4 2 3.1 4.1 3.4 4.7 5.2 7.3 8.6 Visual OK OK Center Density (kg/m3) 68.2 61.3 IFD 25% (N/314cm2) 87 58 CLD25% Hardness (N/cm2) 0.257 0.156 Hardness (%) 22.3 7.2 Tensile strength (kPa) 86 166 Elongation (%) 164 227 Tear strength (N/m) 131 152 Center ball resilience (%) 4 4 Dry compression set (%) 9.2 4.4 30 201037000 Wet compression deformation (%) 8.8 4.6 3.4 2.6 5 4.5 Untested Untested Untested Untested Table 2-2

發泡體箄級60kg/m3 對照例 C1 C2 C3 C4 C5 配方: P 1 (pbw) 55 50 50 31 50 P 2 (pbw) ~ — ~ 10 ~ P 5 (pbw) — — — — — P 6 (pbw) ~ — 50 — -- P 7 (pbw) — 50 ~ 55 50 P 8 (pbw) — — — — — P 9 (pbw) 45 — ~ — — P 10 (pbw) 一 — — — — P 12 (pbw) — — — — ~ P 13 (pbw) ~ — ~ — 3 水(pbw) 1.3 1.3 0.39 0.39 1.3 PEG 400 (pbw) — — 4 4 — DEOA (pbw) ~ — 1.2 1.2 ~ ISO 1指數 90 — — 90 — ISO2指數 — 90 95 — — ISO 3指數 — ~ — — 90 ISO 4指數 — — — — — Niax A-230 (pbw) 0.6 0.6 -- — 0.6 SC (pbw) ~ — 1.15 1.15 ~ DBTDL (pbw) 0.35 — 0.45 0.45 - SO (pbw) — 0.35 — — 0.4 DC 5950 (pbw) 0.25 0.25 1.2 1.2 0.25 發泡體性能: 目視 坍塌 棉花糖 狀泡沫 棉花糖 狀泡沫 坍塌 OK 中心密度(kg/m3) ~ — — — 60.5 IFD 25%(N/314 cm2) — 一 — — 54 CLD 25%硬度 (N/cm2) — — — --1 0.152 硬度變化(%) — — -- — 6.1 拉伸強度(kPa) — — — — 107 伸長(%) — — — — 241 撕裂強度(N/m) — — — -- 124 中心的落球回彈性 (%) — — — — 5 31 201037000 乾壓縮變形(%) 濕壓縮變形(%) • f細㈣對比常見標準發紐配方(對比實關C5)· 了軟質聚氨 • Θ旨低哺發泡IS製射的加王性能、發㈣力學性脉崎$活性。傳統 高不飽和多元醇和DMC低不飽和多元醇_於對比實施例C5。對比實施 例C1-C4僅產生_的或魏“職糖狀”雜塊的發缝,沒有強戶= 能用於進-步發泡體物理性能測試。實施例μιο說明本發明異氛酸ς活性 組合物(b)可提供足夠活性以在軟質聚氨酿低回彈發泡體製備的加成聚合中 與脂肪族或脂職異驗g旨反應,頭得的軟㈣氨自旨低轉發泡體 性能優於傳統由甲笨二異氰酸醋製備的低回彈發泡體(對比實施例C5)。Foam grade kg 60kg/m3 Comparative Example C1 C2 C3 C4 C5 Formulation: P 1 (pbw) 55 50 50 31 50 P 2 (pbw) ~ — ~ 10 ~ P 5 (pbw) — — — — — P 6 ( Pbw) ~ — 50 — -- P 7 (pbw) — 50 ~ 55 50 P 8 (pbw) — — — — — P 9 (pbw) 45 — ~ — — P 10 (pbw) One — — — — P 12 (pbw) — — — — ~ P 13 (pbw) ~ — ~ — 3 Water (pbw) 1.3 1.3 0.39 0.39 1.3 PEG 400 (pbw) — — 4 4 — DEOA (pbw) ~ — 1.2 1.2 ~ ISO 1 Index 90 — 90 — ISO2 Index — 90 95 — — ISO 3 Index — ~ — — 90 ISO 4 Index — — — — — Niax A-230 (pbw) 0.6 0.6 -- — 0.6 SC (pbw) ~ — 1.15 1.15 ~ DBTDL (pbw) 0.35 — 0.45 0.45 - SO (pbw) — 0.35 — — 0.4 DC 5950 (pbw) 0.25 0.25 1.2 1.2 0.25 Foam Performance: Visual collapse of cotton candy foam Marshmallow foam collapse OK Center density (kg/m3 ) ~ — — — 60.5 IFD 25% (N/314 cm2) — A — 54 CLD 25% Hardness (N/cm2) — — — --1 0.152 Hardness Change (%) — — — — 6.1 Tensile Strength (kPa) — — — — 107 Elongation (%) — — — — 241 Tear Strength (N/m) — — — — 124 Center Falling Ball Resilience (%) — — — — 5 31 201037000 Dry Compression Deformation (%) Wet Compression Deformation (%) • f fine (four) contrast common standard hair formula (comparative real C5) · soft polyurethane · Θ 低 low feeding foam IS injection of the king performance, hair (four) mechanical zensaki $ activity. Conventional high unsaturated polyol and DMC low unsaturated polyol - in Comparative Example C5. Comparative Examples C1-C4 produced only the crease of the _ or Wei "glyph" block, and no strong household = could be used for the physical properties test of the progressive foam. EXAMPLES μιο illustrates that the amicotinic acid active composition (b) of the present invention provides sufficient activity to react with an aliphatic or aliphatic acid in an addition polymerization prepared by a soft polyurethane low-rebound foam. The soft (IV) ammonia self-desired low-foaming foam performance of the head is superior to the conventional low-rebound foam prepared by the methyl benzene diisocyanate (Comparative Example C5).

^ 實施例11-JS 、,採用^施m-K)製備中所用的相同步驟製備實施例U_18,所不同的是 1*先使選定❹元醇P3和P4在溫度為6G±lt的烘箱愤化,當多元醇6 全溶化時,接著在進—步發泡之前將多元醇侧制。c的酿室保持^ Ϊ節ίίϊ!^控·23抑㈣—恆溫箱崎敎騎有其他成分 〇 一首先採用Cowles型间剪切混合器以3,〇〇〇rpm在6〇秒内將選定的多 醇P3或P4混合到其他多元醇。通過將表3中所示的組份混合製備實施 _ «氨酿低回彈發泡體。加入有機錫化合物之前,在15升不錄 =杯内減;k概度奴為2,G0Grpm的CGwles魏合器在4()秒内將除了 =錫化合物和異氰_财卜的成分舰合在—起。預混合後,然後將有 =化合物(如果使用)加入杯中,再混合2〇秒,旋轉速度設定為2娜啊。 二後將選疋異亂酸酯化合物加入所得混合物並以3,〇⑻_與所得組合物混 :5 ^姻夺混合物倒入頂部打開的Μ公分(長)χ45公分(寬)恥公分(高) 發泡。泡床達到其最終高度後,讓之在盒中靜止另外十分鐘, 麵所製保存在通風且溫度控制在27±2°C的 名德根據JIS K6400方法(1"7版描述的樣品尺寸,採用實驗室規模電動 鋸機從所製發泡體巾心切糾樣品。接著根據皿Μ⑻方法_版^描 32 201037000 述的樣品尺寸,從指定厚度的發泡體板模切出用於測試撕裂強度、拉伸強 度和伸長的樣品。在進一步物理性能測試之前,使所有樣品在溫度控制在 - 23士 1°C、濕度為50%的恆溫恆濕箱内調節至少24小時。 表^ Example 11-JS, using the same procedure as used in the preparation of mK), Example U_18 was prepared except that the selected quinones P3 and P4 were angered in an oven at a temperature of 6 G ± lt. When the polyol 6 is completely dissolved, the polyol is then side-made before further foaming. c brewing room keeps ^ Ϊ ί ϊ ί ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ ^ 四 四 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温 恒温The polyol P3 or P4 is mixed with other polyols. The preparation was carried out by mixing the components shown in Table 3 - «Ammonia-grown low resilience foam. Before adding the organotin compound, it is subtracted in 15 liters without cup = k is the slave of 2, and the CGwles of the G0G rpm is combined with the composition of the tin compound and the isocyanide in 4 () seconds. Start. After premixing, then add = compound (if used) to the cup, mix for 2 more seconds, and set the rotation speed to 2 Na. After that, the selected chaotic acid ester compound is added to the resulting mixture and mixed with 3, 〇 (8) _ and the resulting composition: 5 ^ marriage mixture is poured into the top open Μ centimeters (length) χ 45 cm (width) shame (high) ) Foaming. After the blister reaches its final height, it is allowed to stand still in the box for another ten minutes. The surface is kept in a ventilated and temperature controlled at 27±2 °C according to the JIS K6400 method (1" The sample was cut from the foamed body by a laboratory-scale electric saw machine, and then cut out from the foam plate of the specified thickness according to the sample size described in the method of Μ (8). Strength, tensile strength and elongation of the sample. All samples were conditioned for at least 24 hours in a constant temperature and humidity chamber controlled at -23 ± 1 °C and 50% humidity before further physical property testing.

3 發泡體箅級60kg/m3 實施例 11 12 13 14 15 16 17 18 配方: P 1 (pbw) 31 31 36 36 21 21 15 17 P 2 (pbw) — — — — 10 10 — ~ P 3 (pbw) — 65 -- 60 -- — 79 79 P 4 (pbw) 65 — 60 - 65 65 ~ — P 13 (pbw) — — — ~ — 2.5 2 2 水(pbw) 0.71 0.71 0.67 0.69 0.55 0.55 0.71 0.71 甘油(pbw) 5 5 5 5 5 5 6 4 DEOA (pbw) 2.4 2.4 2 2.1 1.8 1.8 1 1 ISO 1指數 85 85 90 90 -- — — — ISO 2指數 — — — — 85 85 — — ISO 6指數 ~ — — — — — 85 85 SC (pbw) 0.8 0.8 0.85 0.85 1.0 1.0 0.8 0.8 DBTDL (pbw) 0.36 0.36 0.3 0.33 0.36 0.36 0.54 0.51 DC 5950 (pbw) 1 1.05 1 1.05 0.25 0.25 0.8 0.8 發泡體性能: 目視 0K OK 0K 0K 收縮 OK OK OK 中心密度(kg/m3) 62.3 57.8 60.3 59.8 68.9(*) 61.5 59.2 57.3 IFD 25% (N/314cm2) 67 81 72 69 43(*) 71 92 86 CLD 25%硬度 (N/cm2) 0.204 0.261 0.204 0.208 0.115« 0.196 未測 未測 硬度變化(%) 6.2 6.7 7.1 9.6 13.8 未測 未測 拉伸強度(kPa) 268 294 245 233 315(” 298 286 273 伸長(%) 309 331 287 292 280(*} 264 265 282 撕裂強度(N/m) 296 317 337 351 362(*) 341 389 372 中心的落球回彈性 (%) 7 12 8 10 4(*) 6 11 9 乾壓縮變形 3.1 2.4 3 3.1 8.9r) 6.8 14.6 16.3 濕壓縮變形(%) 2.9 4.7 3.1 2.9 10.1π 7.8 未測 未測 :來自經碾壓後恢復的泡沫樣品的結果 33 201037000 實施例中得到閉孔發泡體,當内部 縮。通過使發顏通過-對電動 / 了1腿開始收 、 動不銹鋼奏b式碾壓破泡機兩次將發泡體碾 ,以防”進收縮。在進_步物理性能測試之前,使經碰發泡體在 溫度控制在23±rc、濕度為5G%的值溫值濕箱内調節至少72小時。實施 例15愧明的物理性能採用從經雜發泡體中心切出的樣品測定。 實施例19-27 通過將表4 t所示組分混合製備實施例π·27的軟質聚氨g旨低回彈發泡 體。抓用實施例1·18製備巾所述的相同步驟製備實施例19_2厂在預混合 步驟中將UV添加細认所得異氰旨活性混合物。3 Foam grade kg60kg/m3 Example 11 12 13 14 15 16 17 18 Formulation: P 1 (pbw) 31 31 36 36 21 21 15 17 P 2 (pbw) — — — — 10 10 — ~ P 3 ( Pbw) — 65 -- 60 -- — 79 79 P 4 (pbw) 65 — 60 — 65 65 ~ — P 13 (pbw) — — — ~ — 2.5 2 2 Water (pbw) 0.71 0.71 0.67 0.69 0.55 0.55 0.71 0.71 Glycerol (pbw) 5 5 5 5 5 5 6 4 DEOA (pbw) 2.4 2.4 2 2.1 1.8 1.8 1 1 ISO 1 Index 85 85 90 90 -- — — — ISO 2 Index — — — — 85 85 — — ISO 6 Index ~ — — — — — 85 85 SC (pbw) 0.8 0.8 0.85 0.85 1.0 1.0 0.8 0.8 DBTDL (pbw) 0.36 0.36 0.3 0.33 0.36 0.36 0.54 0.51 DC 5950 (pbw) 1 1.05 1 1.05 0.25 0.25 0.8 0.8 Foam properties: Visual 0K OK 0K 0K Shrink OK OK OK Center Density (kg/m3) 62.3 57.8 60.3 59.8 68.9(*) 61.5 59.2 57.3 IFD 25% (N/314cm2) 67 81 72 69 43(*) 71 92 86 CLD 25% Hardness (N/cm2) 0.204 0.261 0.204 0.208 0.115« 0.196 Untested hardness change (%) 6.2 6.7 7.1 9.6 13.8 Untested tensile strength (kPa) 268 294 245 233 315 (" 298 286 273 Elongation (%) 309 331 287 292 280 (*} 264 265 282 Tear strength (N/m) 296 317 337 351 362(*) 341 389 372 Center ball return resilience (%) 7 12 8 10 4(*) 6 11 9 Dry compression set 3.1 2.4 3 3.1 8.9r) 6.8 14.6 16.3 Wet compression set (%) 2.9 4.7 3.1 2.9 10.1π 7.8 Untested Untested: Results from foam samples recovered after rolling 33 201037000 Example A closed cell foam is obtained which shrinks when internally. By passing the hair through the - electric / 1 leg start, move the stainless steel b-type crusher to grind the foam twice to prevent "into the contraction. Before the physical performance test, make the The impact foam was conditioned for at least 72 hours in a temperature-controlled wet box with a temperature control of 23 ± rc and a humidity of 5 G%. The physical properties of Example 15 were determined using samples cut from the center of the cross-linked foam. Examples 19-27 The soft polyurethanes of Example π·27 were prepared by mixing the components shown in Table 4 t. The low-rebound foams of Example π·27 were prepared by the same procedure as described in Example 1·18. In Example 19_2, the UV was added to the pre-mixing step to add the carefully identified iso-cyanide active mixture.

除了 UV穩级戦外,按照實施例h8中所示_步驟進行實施例 19-27的發泡體物雌能測試。w穩定性測試中,將1()公分長χ5公分寬 X0.5公分厚的樣品放入内部溫度設定為8〇±1〇c的烘箱内,〇sram ULTRA-VITALUX 300瓦uv燈炮安裝在發泡體樣品正上方3〇公分處。樣 品暴露在紫外光下2G小.與標準灰度卡對比,結果表示為15的等級。 等級5是指根本沒有彥頁色變化,等級i是指幾乎為深色。等級4及以 值表明沒有裸眼可辨別的目視變化。 發泡體箄級301ατ/ττΠ 實施例 19 20 21 22 23 24 25 26 27 配方: P 1 (pbw) 20 20 20 20 40 30 60 cc\ CA P 3 (pbw) 77 _ 76 76 15 15 ou jU P 4 (pbw) — 77 P 11 (pbw) P 13 (pbw) 水(pbw) 甘油(pbw) 1.5 3 1.2 3 0.44 4 0.44 4 45 2 3.45 55 2 3.45 40 2 3.45 40 2 3.45 50 2 3.45 DEOA (pbw) 1.6 1.8 1.2 1.2 1 1 1 ISO 1指數 iso 5指數 85 90 90 95 85 85 1 80 1 90 1 80 SC (pbw) SBC (pbw) 3.75 3.75 3.75 3.75 0.8 0.8 0.8 0.8 0.8 DBI DL (pbw) 0.45 0.45 0.4 0.4 0.28 0.28 0.42 0.42 0.45 34 201037000 DC 5950 (pbw) 0.9 0.9 0.9 0.9 UV 2 2 2 2 發泡體性能: 目視 OK OK OK OK 中心密度(kg/m3) 28.6 31.4 26.3 24.1 IFD 25% (N/314cm2) 37 41 43 56 CLD25%硬度 (N/cm2) 0.106 0.110 0.117 0.149 硬度變化(%) 7.2 8.1 11.6 9.8 拉伸強度(kPa) 196 235 210 217 伸長(%) 287 296 292 258 撕裂強度(N/m) 224 244 267 278 中心的落球回彈性 (%) 6 8 9 11 乾壓縮變形 8.4 5.6 7.4 4.3 濕壓縮變形(%) 8.7 4.7 5.6 5.7 UV穩定性 5 5 5 5 0.8 0.8 0.8 0.83OK29.33811148144143716.1賴 4 0.83 =43=152132160814.1細 4 ΟΚ ΟΚ ΟΚ 28.7 30.6 29.4 30 55 26 0.105 0.149 0.074 19.5 34.8 10.9 164 143 172 142 117 153 153 128 164 4 13 4 9.5 22.6 6.4 14.9 28.7 12.6 4 4 4 貫施例19-27中製備的發泡體說明:公開的異氰酸酯活性混合物可用於 製備密度低至24公斤/立方公尺(約l.5pCf)的不變黃聚氨酯低回彈發泡體。 這些低密度、不變黃聚氨酯低回彈發泡體特別可用於服裝應用,如胸罩墊 和肩墊。 實施例28-30 Ο 通過將表5中所示組分混合製備實施例28-30的軟質聚氨酯低回彈發泡 體。發泡之前,將所有選定成分在溫度控制在23±1。(:的箱内調節至少24 小時。加入有機錫化合物之前,在1.5升不銹鋼杯内採用旋轉速度設定為 l,500rpm的Cowles型混合器在40秒内將除了有機錫化合物和異氰酸醋以 外的成分預混合在一起。預混合後,然後將有機錫化合物(如果使用)加入杯 中,再混合20秒’旋轉速度設定為l,500rpm。然後將選定異氰酸酯化合物 加入所得混合物並以3,OOOrpm與所得組合物混合5秒。立即將混合物倒入 事先預熱到60°C的40公分(長)X40公分(寬)X10公分(高)鋁模具内,模具上 蓋頂端留有4個小孔,將模具溫度維持在60t並蓋上上蓋。將模具溫度保 持在60°C、10分鐘後,將已模塑成型的軟質聚氨酯低回彈發泡體從模具中 取出來,然後在任何進一步測試之前將所製發泡體保存在通風且溫度控 35 201037000 在27±2°C的儲存室内至少72小時。 表5 實施例 __28 配方: --— 30 P 1 (pbw) 20 P 5 (pbw) ·· 25 25 P 8 (pbw) 76 56 35 P 11 (pbw) •亀 — 36 P 12 (pbw) 2 15 水(pbw) 0.6 2 3.5 PEG 400 (pbw) 4 0.54 0.54 DEOA (pbw) 1.68 4 4 ISO 1指數 •爾 1.46 1.55 ISO2指數 95 95 90 SC (pbw) 0.8 一 DBTDL (pbw) 0.55 0.9 0.9 DC 5179 (pbw) 0.9 0.6 0.55 發泡體性能: 0.9 0.84 模壓加工性 可艰壓的 中心密度(kg/m3) __72.6 良好 良好 --—^ 74.7The foam females of Examples 19-27 were tested in accordance with the procedure shown in Example h8 except for UV stabilized enthalpy. In the w stability test, a sample of 1 () cm long χ 5 cm wide and X 0.5 cm thick was placed in an oven with an internal temperature set at 8 〇 ± 1 〇 c, and a sram ULTRA-VITALUX 300 watt uv lamp was installed in the oven. The foam sample is directly above 3 cm. The sample was exposed to UV light at 2 G. Compared to a standard grayscale card, the result was expressed as a rating of 15. Level 5 means that there is no change in the color of the page, and level i means almost dark. Level 4 and values indicate no visual changes that are discernible by the naked eye. Foam grade 301ατ/ττΠ Example 19 20 21 22 23 24 25 26 27 Formulation: P 1 (pbw) 20 20 20 20 40 30 60 cc\ CA P 3 (pbw) 77 _ 76 76 15 15 ou jU P 4 (pbw) — 77 P 11 (pbw) P 13 (pbw) water (pbw) glycerol (pbw) 1.5 3 1.2 3 0.44 4 0.44 4 45 2 3.45 55 2 3.45 40 2 3.45 40 2 3.45 50 2 3.45 DEOA (pbw ) 1.6 1.8 1.2 1.2 1 1 1 ISO 1 index iso 5 index 85 90 90 95 85 85 1 80 1 90 1 80 SC (pbw) SBC (pbw) 3.75 3.75 3.75 3.75 0.8 0.8 0.8 0.8 0.8 DBI DL (pbw) 0.45 0.45 0.4 0.4 0.28 0.28 0.42 0.42 0.45 34 201037000 DC 5950 (pbw) 0.9 0.9 0.9 0.9 UV 2 2 2 2 Foam Performance: Visual OK OK OK OK Center Density (kg/m3) 28.6 31.4 26.3 24.1 IFD 25% (N/ 314cm2) 37 41 43 56 CLD25% hardness (N/cm2) 0.106 0.110 0.117 0.149 Hardness change (%) 7.2 8.1 11.6 9.8 Tensile strength (kPa) 196 235 210 217 Elongation (%) 287 296 292 258 Tear strength (N /m) 224 244 267 278 Center ball return resilience (%) 6 8 9 11 Dry compression deformation 8.4 5.6 7.4 4.3 Wet compression set (%) 8.7 4.7 5.6 5.7 UV stability 5 5 5 5 0.8 0.8 0.8 0.83OK29.33811148144143716.1 Lai 4 0.83 =43=152132160814.1 Fine 4 ΟΚ ΟΚ ΟΚ 28.7 30.6 29.4 30 55 26 0.105 0.149 0.074 19.5 34.8 10.9 164 143 172 142 117 153 153 128 164 4 13 4 9.5 22.6 6.4 14.9 28.7 12.6 4 4 4 The foam prepared in Examples 19-27 illustrates that the disclosed isocyanate-reactive mixture can be used to prepare low-rebound foam of non-yellowing polyurethane with a density as low as 24 kg/m3 (about 1.5 pCf). body. These low density, non-yellowing polyurethane low resilience foams are particularly useful in apparel applications such as bra pads and shoulder pads. Examples 28-30 软 The flexible polyurethane low resilience foams of Examples 28-30 were prepared by mixing the components shown in Table 5. All selected components were controlled at a temperature of 23 ± 1 before foaming. (: Adjust the inside of the box for at least 24 hours. Before adding the organotin compound, use a Cowles type mixer with a rotation speed set to 1,500 rpm in a 1.5 liter stainless steel cup, except for the organotin compound and isocyanuric acid in 40 seconds. The ingredients are pre-mixed together. After pre-mixing, the organotin compound (if used) is then added to the cup and mixed for another 20 seconds. The rotation speed is set to 1,500 rpm. The selected isocyanate compound is then added to the resulting mixture at 3,000 rpm. Mix with the resulting composition for 5 seconds. Immediately pour the mixture into a 40 cm (length) X 40 cm (width) X 10 cm (height) aluminum mold preheated to 60 ° C, leaving 4 small holes in the top of the mold cover. The mold temperature was maintained at 60 t and the lid was capped. After the mold temperature was maintained at 60 ° C for 10 minutes, the molded flexible polyurethane low resilience foam was taken out of the mold and then before any further testing. Store the prepared foam in a ventilated and temperature controlled 35 201037000 in a storage room at 27 ± 2 ° C for at least 72 hours. Table 5 Example __28 Recipe: --- 30 P 1 (pbw) 20 P 5 (pbw) ·· 25 25 P 8 (pbw) 76 56 35 P 11 (pbw) •亀— 36 P 12 (pbw) 2 15 Water (pbw) 0.6 2 3.5 PEG 400 (pbw) 4 0.54 0.54 DEOA (pbw) 1.68 4 4 ISO 1 Index • 1.46 1.55 ISO2 index 95 95 90 SC (pbw) 0.8 A DBTDL (pbw) 0.55 0.9 0.9 DC 5179 (pbw) 0.9 0.6 0.55 Foam performance: 0.9 0.84 Molding processability can be difficult center density (kg/m3 ) __72.6 Good and good ---^ 74.7

G 工業谪用柯 _ 本發明聚氨酯發泡體具有低回彈性 ®細嫩,、雛域物材料 【圖式簡單說明】 益 【主要元件符號說明】 無 36G Industrial 柯 _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _ _

Claims (1)

201037000 七、申請專利範圍: 1. 一種低回彈發泡體’包含以下成份的反應產物: a. —種異1酸酯組分,所述異氰酸酯組分基本不含異氰酸酯 基直接連接到苯環上的芳香族異氰酸酯; b. —種異氰酸酯活性混合物,所述異氰酸酯活性混合物包 含: (bl)第一異氰酸酯活性組分,具有至少26個異氰酸酯活 性基,羥基當量為80_800克, 〇 (b2)第二異氰酸酯活性組分,平均羥基官能度為1.8-6.0, 爹二基^ 1為600-6,000克’第一級(primary)經基含量為至 :>' 30重里份’以所述第二異氰酸酯活性組分經基總重量 為100重量份計, 其中所述第一異氰酸酯活性組分的使用量為2〇_9〇重量 份’所述第二異氰酸酯活性組分的使用量為1〇_8〇重量 份’都以100重量份所述異氰酸酯活性混合物計; c. 催化劑;及 ❹ d.任選地一種或多種選自以下的物質:水、表面活性劑、交 聯劑及添加劑。 2. 如申請專利範圍第丨項所示的發泡體,其中第—異氰酸醋活 性組分具有2.6-6.5個異氰酸酯活性基。 3. 如申清專利範圍第2項所示的發泡體,其中第一異氰酸酯活 性組分具有2.7-5.5個異氰酸酯活性基。 4. 如申請專利範圍第1項所示的發泡體,其中第一異氰酸醋活 性組分之羥基當量為1〇〇_7〇〇克。 5. 如申請專利範圍第4項所示的發泡體,其中第_異氰酸g旨活 性組分之羥基當量為90-510克。 37 201037000 6·如申請專利範圍第1項所示的發泡體,其中第二異氰酸酯活 性組分之平均羥基官能度為1.85-4.5。 彳 7.如申請專利範圍第1項所示的發泡體,其中第二異氰酸酯活 性組分之羥基當量為800-4,500克。 4 8.如申請專利範圍第丨項所示的發泡體,其中第二異氰酸酯活 性組分之第一級經基含量為至少40重量份,以所述第二異 氰酸酯活性組分羥基總重量為1〇〇重量份計。 “ 9.如申凊專利範圍第8項所示的發泡體,其中第二異氰酸酯活 Ο ❹ 芑組分之第一級經基含量為至少51重量份,以ί斤述第I異 氰酸醋活性組分經基總重量為100重量份計。 、 10.如申請專利範圍第1項所示的發泡體,其中所述第一異氰萨 醋活性組分的使用量為2G_7()重量份,所述第二異“ 性組分的使用量為30-80重量份,均以100重量份所述里 酸酯活性混合物計。 ν、鼠 1·=,專利範圍第i項所示的發泡體,其中所述異氰酸醋电 選自一種或多種以下的異氛酸醋:脂肪族異氛酸醋、 月曰裱族異氰酸酯和異氰酸酯基不直接連接到苯環上的 族異氰酸酯。 曰 12’圍第11項所示的發泡體,其中所述脂肪族異 體Y異級料體或脂_多異氰酸醋單 胆·和二聚體的共混物;其中: 述;, f f :列至少-種多異氰酸酯經三聚反應的產 直接、脂環族多異氰酸酯或異氰酸酯基不 直接連接到苯環上的芳香族多異氰酸酯; ,述共混物中的NCO含量為2〇 5·5〇 gt 組分中100重量份總異氰_旨計;且里知叫氰酉文酉曰 平均計算官能度為2-3。 38 201037000 所示的發泡體,其中所述脂肪族異 亞甲二之 少一種:六亞曱基二異氰酸酯、六 萨H細1、十一烷三異氰酸酯、+-烷二異氰西: 面曰、其二聚體和三聚體。 氮酉文 14_ϊ!ϊίϊί圍第12項所示的發泡體,其中所述脂肪族多 ί ϋ 亞甲基二異氰咖旨,所述三聚體為六亞甲基^ 異鼠酸酯三聚反應的產物。 7丞一 11項所示的發泡體,其中所述脂環族里201037000 VII. Patent Application Range: 1. A low-rebound foam 'reaction product containing the following components: a. an iso-I-ester component, the isocyanate component is substantially free of isocyanate groups and is directly attached to the benzene ring. An aromatic isocyanate; b. an isocyanate reactive mixture comprising: (bl) a first isocyanate active component having at least 26 isocyanate reactive groups, a hydroxyl equivalent weight of 80-800 grams, bismuth (b2) The diisocyanate active component has an average hydroxyl functionality of 1.8-6.0, and the fluorenyl group 1 is 600-6,000 g. The 'primary base content is: to: '30 aliquots' to the second The isocyanate-reactive component is used in an amount of 100 parts by weight based on the total weight of the base, wherein the first isocyanate-reactive component is used in an amount of 2 〇 9 9 parts by weight 'the second isocyanate-reactive component is used in an amount of 1 〇 8 parts by weight 'based on 100 parts by weight of the isocyanate reactive mixture; c. catalyst; and ❹ d. optionally one or more selected from the group consisting of water, surfactants, crosslinkers Additives. 2. A foam as set forth in the scope of the patent application, wherein the first isocyanate-reactive component has from 2.6 to 6.5 isocyanate reactive groups. 3. The foam of claim 2, wherein the first isocyanate reactive component has from 2.7 to 5.5 isocyanate reactive groups. 4. The foam of claim 1, wherein the first isocyanate active component has a hydroxyl equivalent weight of from 1 to 7 g. 5. The foam according to claim 4, wherein the hydroxyl group equivalent of the active component of the cyanuric acid is 90-510 g. 37 201037000 6. The foam of claim 1, wherein the second isocyanate reactive component has an average hydroxyl functionality of from 1.85 to 4.5.彳 7. The foam of claim 1, wherein the second isocyanate reactive component has a hydroxyl equivalent weight of from 800 to 4,500 g. 4. The foam according to claim 2, wherein the second isocyanate active component has a first stage base group content of at least 40 parts by weight, based on the total weight of the second isocyanate active component hydroxyl group. 1 〇〇 by weight. 9. The foam of claim 8, wherein the second isocyanate active hydrazine component has a first stage base content of at least 51 parts by weight, and the first isocyanate is The vinegar active component is 100 parts by weight based on the total weight of the base. 10. The foam according to claim 1, wherein the first isocyansone active component is used in an amount of 2 G_7 (). The second heterogeneous component is used in an amount of from 30 to 80 parts by weight, based on 100 parts by weight of the lysate active mixture, by weight. ν, 鼠1·=, the foam shown in the item i of the patent range, wherein the isocyanate vinegar is selected from one or more of the following sulphuric acid vinegar: aliphatic sulphuric acid vinegar, Yuelu The isocyanate and isocyanate groups are not directly attached to the family isocyanate on the phenyl ring.发泡12', the foam of the eleventh item, wherein the aliphatic allogeneic Y heterogeneous material or a blend of a fat-polyisocyanate mono- and dimer; wherein: Ff : an aromatic polyisocyanate in which at least one polyisocyanate is trimerized to produce a direct, alicyclic polyisocyanate or isocyanate group which is not directly bonded to the benzene ring; the NCO content in the blend is 2〇5 • 100 parts by weight of total isocyanide in the 5 〇 gt component; and the average calculated functionality of cyanoguanidine is 2-3. 38 201037000 The foam shown in which one of the aliphatic iso-methylene groups is one of: hexamethylene diisocyanate, hexa H fine 1, undecane triisocyanate, +-alkaned diisocyanide:曰, its dimers and trimers. The foam shown in item 12, wherein the aliphatic polymethylene diisocyanate is a hexamethylene group The product of the polymerization. a foam shown in Item 11 of the above, wherein the alicyclic group ^ 3脂環族多異氰酸醋單體或脂環族多異氰酸酉旨i 體和二聚體的共混物;其中: 早 =三為選自下列至少—種多異氰酸醋三聚反應的生成 ί 9氰酸Ϊ、脂環族多異氰_或異氰咖旨ί 不直接連接到本環上的芳香族多異氰酸酯; 〔斤巧混物中的NCO含量為20.5-38.0重量份,以異氛酸酉匕 、、且/刀中100重量份總異氰酸酯計;且 _ —曰 平均計算官能度為2-3。 16.=請專利細第15項所示的發泡體,其中所述脂環族異 包含,自以下的至少一種:雙環庚烧三異氛酸醋、、異 佛爾,二異氰酸醋、二環己基甲烧二異氰酸酷、甲基環己& 二異氰酸自旨、二曱基環己垸二異氰酸g旨、其二聚體和三聚體= Η.如^請專利範圍第15項所示的發泡體’其巾所述脂環族多 異氰酸酯為異佛爾酮二異氰酸酯,所述三聚體為六亞曱基二 異乱酸S旨三聚反應的產物。 18.如申請專利範@第u項所示的發泡體’其中所述異氮酸醋 基不直接連制苯環上的芳香族異氰酸酯包含異氰酸醋基 不直接連接到苯環上的芳香族多異氰酸醋單體或異氮酸醋 基不直接連接到苯環上的芳香族多異氰酸酯單體和三聚體 39 201037000 的共混物;其中: 選自下列至少—種多異氰酸酯三聚反應的生成 m Γ ΐ族f異氰酸醋、脂環族多異氰酸喊異氰酸醋基 、到笨環上的芳香族多異氰酸酯; f 混物中的NCQ含量為2α5·44Ό重量份,以異氣酸醋 、,且/刀中100重量份總異氰酸酯計;且 平均計算官能度為2-3。 Ο ο 19.ί 圍第18項所示的發泡體,其中所述異氰酸酿 =一# . — ί妾到苯裱上的芳香族異氰酸酯為選自以下的至 ^ 本一亞甲基—異氰酸酯、四曱基苯二亞曱基二里1 酸酯、其二聚體和三聚體。 ,、氰 2〇·2Ϊί1祀圍第18項所示的發泡體,其中所述異氰酸酿 基Ϊ直fjf到芳環上的芳香族多異氰酸醋為苯二亞甲i 笨二亞曱基二異議,所述三聚^ 八亞曱基一異鼠g文g曰二聚反應的產物。 21. 如申π專利範圍第1項所示的發泡體,其中所述第一 酯活性組分(bl)為聚環氧两燒,且二I馱 基,不飽和度低於0.05=。具有至)3個異纖旨活性 22. t申請專利範圍第1項所示的發泡體,其中所述第-異氦, 酉曰活性組分(bl)為聚環氧丙烧,該^ i ’由雙金屬氰化轉合物催化的 哀口成U ’且不飽和度低於〇 〇2〇meq/g。 23. 如申請專利範圍第!項所示的免泡體,其 酉旨活性組分(b2)為聚(四亞甲基峻)二醇,重= l,2^0-2,400g/m〇l ’所述第二異氛酸酉旨活性組-刀 羥基官能團為第一級羥基。 刀(的所有 24. 如申請專利範圍第1項所示的發泡體,其中所述第二異氰 201037000 酯活性組分(b2)為聚(三亞甲基醚)二醇,重均分子量為 1,20(K3,000 g/m〇i,所述第二異氰酸g旨活性組分(b2)中的ς 輕基g能困為第^一級經基。 25.如申請專利範圍第〗項所示的發泡體,其中所述第二異氰酽 ,活性組f(b2)為聚(環氧乙烧_環氧丙烷)共聚物’包含丄 少7.5重量份環氧乙烷,以1〇〇重量份所述第二異氰醆 性組分計。^ 3 alicyclic polyisocyanate monomer or alicyclic polyisocyanate is a blend of i and dimer; wherein: early = three is selected from the following at least one type of polyisocyanate The formation of a trimerization reaction ί 9 cyanate, alicyclic polyisocyanate or isocyanate ί is not directly attached to the aromatic polyisocyanate on the ring; [NCO content in the mixture is 20.5-38.0 Parts by weight, based on hydrazine hydrate, and / 100 parts by weight of total isocyanate in the knives; and _ 曰 average calculated functionality of 2-3. 16. The foam according to the fifteenth aspect of the invention, wherein the alicyclic group comprises at least one of the following: bicycloheptane triisoacetate, isophor, diisocyanate , dicyclohexyl carbaryl diisocyanate, methylcyclohexan & diisocyanate, dimercaptocyclohexyl diisocyanate g, its dimer and trimer = Η. ^Please refer to the foam shown in item 15 of the patent range. The alicyclic polyisocyanate of the towel is isophorone diisocyanate, and the trimer is a trimerization reaction of hexamethylene bis-isosuccinic acid S. Product. 18. The foam as described in the patent specification @u, wherein the isoammonic acid vine group is not directly bonded to the aromatic isocyanate on the benzene ring, and the isocyanate group is not directly bonded to the benzene ring. a blend of an aromatic polyisocyanate monomer or an isocyanate group which is not directly bonded to an aromatic polyisocyanate monomer and a trimer 39 201037000 on a benzene ring; wherein: at least one of the following polyisocyanates is selected from the group consisting of The formation of the trimerization reaction m Γ ΐ f isocyanate vinegar, alicyclic polyisocyanate, isocyanate vinegar, aromatic polyisocyanate on the stupid ring; the NCQ content in the f mixture is 2α5·44Ό Parts by weight, based on 100 parts by weight of total isocyanate in isogastric acid vinegar, and / knife; and the average calculated functionality is 2-3. ο ο ί ί ί ί ί ί ί ί ί ί ί ί 19. 19. 19. 19. ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί ί - isocyanate, tetradecyl benzodiamidino sulphate, dimers and trimers thereof. , Cyanide 2〇·2Ϊί1祀 The foam shown in Item 18, wherein the isocyanic acid Ϊ straight fjf to the aromatic ring on the aromatic polyisocyanate is benzodiacene i In the case of arsenic, the product of the dimerization reaction of the trimeric octapeptide. 21. The foam of claim 1, wherein the first ester active component (bl) is a polyepoxy two-burning, and a di-indenyl group having an unsaturation of less than 0.05 =. The foam shown in the first item of claim 2, wherein the first-isoindole, the active component (bl) is a polyglycolide, the ^ i' is catalyzed by a double metal cyanide conversion to U' and the degree of unsaturation is less than 〇〇2〇meq/g. 23. If you apply for a patent scope! The bubble-free body shown in the item, wherein the active component (b2) is poly(tetramethylene sulphate) diol, and the weight = l, 2^0-2, 400 g/m〇l The acid-acting group-knife hydroxyl functional group is a first-order hydroxyl group. All of the foams of the invention, wherein the second isocyanide 201037000 ester active component (b2) is poly(trimethylene ether) glycol, and the weight average molecular weight is 1,20 (K3,000 g/m〇i, the second isocyanate g of the active component (b2) in the active component (b2) can be trapped as the first-order meridine. 25. The foam shown in the item, wherein the second isocyanide, the active group f(b2) is a poly(ethylene oxide-propylene oxide) copolymer containing less than 7.5 parts by weight of ethylene oxide. The amount of the second isocyanato component is 1 part by weight. 6.如申請專利範圍帛25項所示的發泡體,其中所述第二 _旨活性組分(b2)為聚(環氧乙烧_環氧丙烧)共聚物二’醇, 不飽和,低於〇.〇5meq/g,第一級羥基含量超過51%重量, 以所述第一異氰酸酯活性組分(b2)中總羥基的重量計。 7. t申請ί利範圍第1項所稍發泡體,射所敍聯劑的重 能^子4為6〇_420 g/m〇1 ’並具有至少兩個異氰酸自旨活性官 28. 專利範圍第i項所示的發泡體,其中所述交聯劑的使 物^為〇·245重量份’以100重量份所述異氰酸醋活性混合 9 圍第f8項所示的發泡體,其中所述交聯劑的 合物# I _12重量份,以1〇〇重量份所述異氰酸酯活性混 性1項所示的發泡體’其中所述異氰酸醋活 計^ ί重量份(α 100重量份異氰酸醋活性組分 重旦物多元醇的固含量為5·55 ΚΟΗ/g 〇 U 重篁份聚合物多元醇計,經基值為15_50 mg 3l.如申請專利範圍第1 性系且分還包含0-5.0 項所示的發泡體,其中所述異氰酸酯活 重量份(以100重量份發泡體總重量計) 41 201037000 為開孔劑’所述聚環氧秘的名義經基 吕月匕度為1,重均分子量為800_8,500g/m〇1。 31項所示的發泡體,其中所述異氛酸醋 1、刀3 〇·3·5重量份(以100重量份發泡體總重量 丙烧(b3)作為開孔劑’所述聚環氧丙烧“名義 羥基吕此*度為1,重均分子量為800-8,500 g/mol。 ❹ Ο 33. tTf專利範圍第1項所示的發泡體,其中所述催化劑W 為k自下列至少一種與有機金屬催化劑的混合物:布忍司 (Bronsted)酸與驗金屬的鹽類或布忍司特酸與鹼土金屬的鹽 類。 疏 34. 如申請專利範圍第33項所示的發泡體,其中所述布忍 酸與驗金屬的鹽類為碳酸氫納。 35. 如申請專利麵第33項所示的發泡體,其中所述布忍 酸與驗金屬的鹽類為碳酸鈉。 36. 如申請專利範圍第1項所示的發泡體,其中所述交聯劑為式 I化合物 H(3-X)-N-[(CH2)2-OH]x 其中X為1-3的整數。 37. 如申請專利範圍第36項所示的發泡體,其中所述交聯 二乙醇胺。 38_ —種製備低回彈發泡體的方法,包括在異氰酸酯指數為約 65-110下使包含以下成份的反應物,進行反應: …… a. —種異氰酸酯組分,所述異氰酸酯組分基本不含異氰酸酽 基直接連接到本壤上的芳香族異氰酸酯; * b. —種異氰酸酯活性混合物,所述異氰酸酯活性混合物 含: 42 201037000 (bl)第一異氰酸酯活性組分,具有至少2 6個異氰酸酯活 性基,羥基當量為80-800克, (b2)第二異氰酸酯活性組分’平均羥基官能度為1.8-6.0, 罗至基當里為600-6,000克,第一級(primary)經基含量為至 少30重量份,以所述第二異氰酸酯活性組分羥基總重量 為100重量份計, 其中所述第一異氰酸酯活性組分的使用量為20-90重量 份’所述第二異氰酸酯活性組分的使用量為1〇_80重量 份’都以100重量份所述異氰酸酯活性混合物計; c.催化劑;及 d·任選地一種或多種選自以下的物質:水、表面活性劑、交 聯劑及添加劑。 39. 如申請專利範圍第38項所示的方法,其中第一異氰酸酯活 性組分具有2.6-6.5個異氰酸g旨活性基。 40. 如申請專利範圍第39項所示的方法,其中第一異氰酸酯活 性組分具有2.7-5.5個異氰酸酯活性基。 41. 如申請專利範圍第38項所示的方法,其中第一異氰酸酯活 性組分之羥基當量為100-700克。 42. 如申請專利範圍第41項所示的方法,其中第一異氰酸酯活 性組分之羥基當量為90-510克。 43. 如申請專利範圍第38項所示的方法’其中第二異氰酸酯活 性組分之平均羥基官能度為1.85-4.5。 44. 如申請專利範圍第38項所示的方法,其中第二異氰酸酯活 性組分之羥基當量為800-4,500克。 45·如申^專利範圍第38項所示的方法,其中第二異氰酸酯活 性組分之第一級羥基含量為至少40重量份,以所述第二異 43 201037000 氰酸酯活性組分經基總重量為1〇〇重量份計。 46. 如申請專利範圍第45項所示的方法,其中第二異氰酸酯活 性組分之第一級羥基含量為至少51重量份,以所述第二異 氰酸酯活性組分羥基總重量為iOO重量份計。 47. 如申請專利範圍第38項所示的方法,其中所述第一異氰醆 醋活性組分的使用量為20-70重量份,所述第二異氰酸S旨活 性組分的使用量為30-80重量份,均以1〇〇重量份所述異氰 酸酉旨活性混合物計。 48. 如申請專利範圍第%項所示的方法,其中所述發泡體在異 氰酸酯指數為約75-105下製備。 49. 如申請專利範圍第38項所示的方法,其中所述異氰酸酯組 選自一種或多種以下的異氰酸醋:脂肪族異氰酸醋、 脂環族異氰酸酯和異氰酸酯基不直接連接到苯環上的关 族異氰酸酯。 货 5〇_如申請專利範圍第49項所示的方法,其中所述脂肪族 酸酯包含脂肪族多異氰酸酯單體或脂肪族多異氰酸酯 和三聚體的共混物;其中: 所述三聚體為選自下舰少—種多異氰_經三聚反應的產 物、·脂肪族多異氰酸醋、脂環族多異氰酸醋或異氰酸酿基不 接連接到笨環上的芳香族多異氰酸酯; 所述共混物中的NCO含量為20.5-50.0重量份,以異氰酸酉t 組分中100重量份總異氰酸酯計;且 9 平均計算官能度為2-3。 51.如申睛專利範圍第5〇項所示的方法,其中所述脂肪族異氰 酸酯^含選自以下的至少一種:六亞曱基二異氰酸酯、六亞 甲基二異氰酸酯、一烷三異氰酸酯、十一烷二異氰酸酯、 其一聚體和三聚體。 44 201037000 52. 如申請專利範圍第5〇項所示的方法’其中所述脂肪族多異 氰酸酯為六亞曱基二異氰酸酯,所述三聚體為六亞曱基二異 fL酸醋三聚反應的產物。 53. 如申請專利範圍第49項所示的方法,其中所述,環族異氰 酸酯包含脂環族多異氰酸酯單雜戒脂環族多異氰酸酯單體 和三聚體的共混物;其中:6. The foam according to claim 25, wherein the second active component (b2) is a poly(epoxypyrene-epoxypropane) copolymer bis-alcohol, unsaturated , less than me.〇5meq/g, the first-stage hydroxyl content exceeds 51% by weight, based on the weight of the total hydroxyl groups in the first isocyanate-reactive component (b2). 7. t Apply for the foam in the first item of the ί利 range, the weight of the sedative agent 4 is 6 〇 420 420 g / m 〇 1 ' and has at least two isocyanic acid 28. The foam of item i of the patent scope, wherein the cross-linking agent of the cross-linking agent is 245·245 parts by weight', as shown in item f8 of 100 parts by weight of the isocyanuric acid active mixture The foam, wherein the crosslinking agent is a compound # I _12 parts by weight, and the foam represented by the isocyanate-active mixture of 1 part by weight of the isocyanate vinegar ί parts by weight (α 100 parts by weight of isocyanate vinegar active component heavy denier polyol has a solid content of 5·55 ΚΟΗ / g 〇 U 篁 聚合物 part of the polymer polyol, the base value is 15_50 mg 3l. Patent Application No. 1 is also a foam comprising the 0-5.0 item, wherein the isocyanate parts by weight (based on 100 parts by weight of the total foam) 41 201037000 is a cell opener The name of the polyepoxy secret is 1. The weight average molecular weight is 800_8,500 g/m〇1. The foam shown in item 31, wherein the sulphuric acid vinegar 1, the knife 3 〇·3 · 5 parts by weight (based on 100 parts by weight of the total weight of the foam, c-boiled (b3) as a cell opener'. The polyglycolate "nominal hydroxyl group is 1 degree, and the weight average molecular weight is 800-8,500 g /发泡 Ο 33. The foam of the first aspect of the tTf patent, wherein the catalyst W is a mixture of at least one of the following and an organometallic catalyst: a Bronsted acid and a metal salt or A salt of bromide acid and an alkaline earth metal. A foam according to claim 33, wherein the salt of the acid and the metal salt is sodium hydrogencarbonate. The foam according to Item 33, wherein the salt of the acid and the metal is sodium carbonate. 36. The foam according to claim 1, wherein the crosslinking agent is Formula I. The compound H(3-X)-N-[(CH2)2-OH]x wherein X is an integer of 1-3. 37. The foam of claim 36, wherein the cross-linking Ethanolamine 38_ is a method for preparing a low resilience foam comprising: reacting a reactant comprising the following components at an isocyanate index of about 65-110 Reaction: a. isocyanate component, the isocyanate component is substantially free of aromatic isocyanate directly attached to the soil by the isocyanate group; * b. isocyanate active mixture, the isocyanate active mixture Contains: 42 201037000 (bl) a first isocyanate active component having at least 26 isocyanate reactive groups having a hydroxyl equivalent weight of from 80 to 800 grams, (b2) a second isocyanate reactive component having an average hydroxyl functionality of from 1.8 to 6.0, The base is contained in an amount of from 600 to 6,000 g, the primary base content is at least 30 parts by weight, based on 100 parts by weight of the total weight of the second isocyanate active component hydroxyl group, wherein the first isocyanate The active component is used in an amount of from 20 to 90 parts by weight 'the second isocyanate-reactive component is used in an amount of from 1 to 80 parts by weight' based on 100 parts by weight of the isocyanate-activated mixture; c. a catalyst; Optionally, one or more materials selected from the group consisting of water, surfactants, crosslinking agents, and additives. 39. The method of claim 38, wherein the first isocyanate reactive component has from 2.6 to 6.5 isocyanate g reactive groups. 40. The method of claim 39, wherein the first isocyanate reactive component has from 2.7 to 5.5 isocyanate reactive groups. 41. The method of claim 38, wherein the first isocyanate reactive component has a hydroxyl equivalent weight of from 100 to 700 grams. 42. The method of claim 41, wherein the first isocyanate reactive component has a hydroxyl equivalent weight of from 90 to 510 grams. 43. The method of claim 38, wherein the second isocyanate reactive component has an average hydroxyl functionality of from 1.85 to 4.5. 44. The method of claim 38, wherein the second isocyanate reactive component has a hydroxyl equivalent weight of from 800 to 4,500 grams. 45. The method of claim 38, wherein the second isocyanate active component has a first stage hydroxyl group content of at least 40 parts by weight, and the second iso 43 201037000 cyanate ester active component is based on The total weight is 1 part by weight. 46. The method of claim 45, wherein the second isocyanate active component has a first stage hydroxyl group content of at least 51 parts by weight based on the total weight of the second isocyanate active component hydroxyl group of iOO parts by weight. . 47. The method of claim 38, wherein the first isocyanuric acid active component is used in an amount of from 20 to 70 parts by weight, and the second isocyanate is used as an active component. The amount is from 30 to 80 parts by weight, based on 1 part by weight of the isocyanate-based active mixture. 48. The method of claim 5, wherein the foam is prepared at an isocyanate index of from about 75 to about 105. 49. The method of claim 38, wherein the isocyanate group is selected from one or more of the following isocyanate: aliphatic isocyanate, alicyclic isocyanate, and isocyanate are not directly attached to benzene Guanzu isocyanate on the ring. The method of claim 49, wherein the aliphatic acid ester comprises an aliphatic polyisocyanate monomer or a blend of an aliphatic polyisocyanate and a trimer; wherein: the trimer The body is selected from the following ships: a polyisocyanate-product of the trimerization reaction, an aliphatic polyisocyanate vinegar, an alicyclic polyisocyanate vinegar or an isocyanate aryl group is not connected to the awkward ring The aromatic polyisocyanate; the NCO content in the blend is from 20.5 to 50.0 parts by weight, based on 100 parts by weight of the total isocyanate in the yttrium isocyanate component; and the average calculated functionality is 2-3. 51. The method of claim 5, wherein the aliphatic isocyanate comprises at least one selected from the group consisting of hexamethylene diisocyanate, hexamethylene diisocyanate, monoalkyl triisocyanate, Undecane diisocyanate, its monomer and trimer. 44 201037000 52. The method of claim 5, wherein the aliphatic polyisocyanate is hexamethylene diisocyanate, and the trimer is a trimerization reaction of hexamethylene diiso-fL acid vinegar Product. 53. The method of claim 49, wherein the cycloisocyanate comprises a blend of an alicyclic polyisocyanate monocyclic cycloaliphatic polyisocyanate monomer and a trimer; Ο 所述三聚體為選自下列至少一種多異氰酸酯三聚反應的生成 產物:脂肪族多異氰酸酯、脂環族多異氰酸酯或異氰酸酯基不直 接連接到笨環上的芳香族多異氰酸酯; 所述共混物中的NCO含量為20.5-38.0重量份,以異氰酸酯 組分中100重量份總異氰酸酯計;且 平均計算官能度為2-3。 54. 如申請專利範圍第53項所示的方法,其中所述脂環族異氰 酸酯包含選自以下的至少一種:雙環庚烷三異氰酸酯、異佛 爾酮二異氰酸酯、二環己基甲烷二異氰酸酯、甲基環己烷二 異氰酸酯、二甲基環己烷二異氰酸酯、其二聚體和三聚體。 55. 如申請專利範圍第53項所示的方法,其中所述脂環族多異 氰酸酯為異佛爾酮二異氰酸酯,所述三聚體為六亞曱基二異 氰酸酯三聚反應的產物。 56. 如申請專利範圍第49項所示的方法,其中所述異氰酸酯基 不直接連接到苯環上的芳香族異氰酸酯包含異氰酸酯基不 直接連接到苯環上的芳香族多異氰酸酯單體或異氰酸酯基 不直接連接到苯環上的芳香族多異氰酸酯單體和三聚 共混物;其中: 所述三聚體為選自下列至少-種多異氰酸酿三聚反應的生成 產物:脂肪族多異氰酸酯、脂環族多異氰酸自旨或& 不直接連制«上的料衫魏 45 201037000 所述共混物中的NCO含量為20.5-44.0重量份,以異氰酸酯 組分中100重量份總異氰酸酯計;且 平均計算官能度為2-3。 57·如申請專利範圍第56項所示的方法,其中所述異氰酸酯基 不直接連接到本ί衣上的芳香族異乳酸I旨為選自以下的至少 種·本一亞曱基二異氰酸醋、四甲基笨二亞曱基二異氰酸 酯、其二聚體和三聚體。 土一、 Ο Ο 8.如申凊專利棚第56項所示的方法,其巾所述異氰酸醋基 不直接連接到芳環上的芳香族多異氰酸酯為苯二亞甲其二 甲基苯二亞甲基二異氰酸醋“ 亞曱基二異亂酸酯三聚反應的產物。 59. ^申請專利範圍第38項所示的方法,其中所述 酉曰活性組分(M)為聚環氧丙烧,具# = 基,不飽和度低於0.05meq/g。 ⑽亂W曰活性 60. 如申請專利範圍第38項所示的方法, 醋活性組分(bl)為聚環氧丙烧,具有至少、$異鼠西夂 基,由雙金屬氰化物螯合物催化的 個異减酯活性 備,且不飽和度低於0.020nfeq^;W丙烧開環加成聚合製 61. 如申請專利範圍第38項所示的 醋活性組分⑽為聚(四亞甲基,醇中所^第酸 1,200-2,400#111〇1,所述第二里奢缺^—知,重均分子量為 羥基官能團為第一級羥基。"—文®曰活性組分(b2)中的所有 幻.如申請專利範圍第38項所示的 、… 酯活性組分(b2)為聚(三亞甲茂秘二二中所述第二異氰酸 1,200-3,00(^/111〇1,所述第_| = ~)二醇,重均分子量$ 經基官能團為第-級異·轉活性組分_中的所^ 63,如申請專利範圍第38項 所不的方法,其中所述第二異氦酸 46 201037000 ,活性組分(b2)為聚(環氧乙烷-環氧丙烷)共聚物,包含至 少7.5重量份環氧乙烷,以100重量份所述第二異氰酸酯活 性組分計。 64. 如申請專利範圍第63項所示的方法,其中所述第二異氰酸 酯組分(b2)為聚(環氧乙烷-環氧丙烷)共聚物二醇,通 ,環氧丙烷加成聚合到具有2個羥基的引發劑上,然後用環 氧^烷封端而製備,不飽和度低於〇 〇5 meq/g,第一級羥基 合1超過51%重量,以所述第二異氰酸酯活性組分(b2)中總 羥基的重量計。Ο the trimer is a product of a trimerization reaction of at least one polyisocyanate selected from the group consisting of an aliphatic polyisocyanate, an alicyclic polyisocyanate or an aromatic polyisocyanate in which an isocyanate group is not directly bonded to a stupid ring; The NCO content of the mixture is from 20.5 to 38.0 parts by weight based on 100 parts by weight of the total isocyanate in the isocyanate component; and the average calculated functionality is 2-3. 54. The method of claim 53, wherein the alicyclic isocyanate comprises at least one selected from the group consisting of biscycloheptane triisocyanate, isophorone diisocyanate, dicyclohexylmethane diisocyanate, Cyclohexane diisocyanate, dimethylcyclohexane diisocyanate, dimers and trimers thereof. 55. The method of claim 53, wherein the alicyclic polyisocyanate is isophorone diisocyanate, and the trimer is a product of trimerization of hexamethylene diisocyanate. 56. The method of claim 49, wherein the aromatic isocyanate in which the isocyanate group is not directly bonded to the benzene ring comprises an aromatic polyisocyanate monomer or isocyanate group which is not directly bonded to the benzene ring. An aromatic polyisocyanate monomer and a trimerized blend which are not directly bonded to a benzene ring; wherein: the trimer is a product of at least one of the following polyisocyanate trimerization reactions: aliphatic Isocyanate, alicyclic polyisocyanate, or <not directly connected to the top of the shirt, Wei 45 201037000, the NCO content of the blend is 20.5-44.0 parts by weight, 100 parts by weight of the isocyanate component Total isocyanate count; and the average calculated functionality is 2-3. 57. The method according to claim 56, wherein the aromatic isocyanate in which the isocyanate group is not directly bonded to the present coating is at least one selected from the group consisting of the following sub-indenyl diisocyanide. Sour vinegar, tetramethyl stilbene diisocyanate, dimers and trimers thereof.土一, Ο Ο 8. The method shown in item 56 of the patent shed, the aromatic polyisocyanate in which the isocyanate group is not directly bonded to the aromatic ring is benzodiamidethylene dimethyl a product of a trimerization reaction of a decylene diisocyanate vinegar "n-decyl diisomeric acid ester." 59. The method of claim 38, wherein the hydrazine active component (M) It is a polyglycidil, with # = base, and the degree of unsaturation is less than 0.05 meq/g. (10) Chaos W曰 activity 60. As shown in the method of claim 38, the vinegar active component (bl) is agglomerated. Epoxy propylene, having at least, an isoindole, an isoxived ester activity catalyzed by a double metal cyanide chelate, and having an unsaturation of less than 0.020 nfeq^; W-propane ring-opening addition polymerization 61. The vinegar active component (10) as shown in item 38 of the patent application is poly(tetramethylene, the acid in the alcohol, 1,200-2,400#111〇1, the second nickname is missing ^ - know that the weight average molecular weight is a hydroxyl functional group which is a first-order hydroxyl group. All the phantoms in the active component (b2) are as shown in claim 38 of the patent application range. The component (b2) is a poly(1,200-3,00 (^/111〇1, the _|=~) diol of the second isocyanate described in the methylene phthalocene bis 22 The method wherein the molecular weight functional group is a first-order iso-trans-active component, as described in claim 38, wherein the second isononic acid 46 201037000, the active component (b2) And a poly(ethylene oxide-propylene oxide) copolymer comprising at least 7.5 parts by weight of ethylene oxide, based on 100 parts by weight of the second isocyanate active component. 64. The method wherein the second isocyanate component (b2) is a poly(ethylene oxide-propylene oxide) copolymer diol, and a propylene oxide addition polymerization is carried out to an initiator having two hydroxyl groups. Then prepared by capping with epoxy oxide, the degree of unsaturation is less than 〇〇5 meq/g, the first-stage hydroxyl group is more than 51% by weight, and the total hydroxyl group in the second isocyanate-reactive component (b2) Weight meter. 65. 如申凊專利範圍第38項所示的方法,其中所述交聯劑的重 均分子量為60-420 g/mol,並具有至少兩個異氰酸酯活性官 能團; 66. 如^專利細第38項所示的方法,其巾所述交聯劑的使 用量為0.2-15重量份’以100重量份所述異氰酸醋活性混合 67.如申μ專利範圍第66項所示的方法,其中所述交聯劑的使 =量為1.2-12重量份’ α 100重量份所述異氰酸醋活性混合 物計。 6^申請專利細第38項所示的絲,其_所述異氰麵活 刀還包含〇_4〇重量份(上乂 1〇〇重量份異氛酸醋活性組分 計)之聚合物多元醇,所述聚合物多元醇 重量份,以10。重量份聚合物多元醇計,絲固值二二 KOH/g 〇 圍第38項所示的方法,針所述異氰酸醋活 夕匕3 0-5.0重量份(以100重量份發泡體總重量計) ίίΐϊ丙院(b3)作為開孔劑,所述聚環氧丙烧的名義經基 吕月b度為1,重均分子量為800-8,500g/md。 47 201037000 70.如申請專利範圍第69項所示的方法,其中所述異氰酸酯活 性組分還包含〇_3 5重量份(以〗〇〇重量份發泡體總重量計) - 之聚環氧丙烧(b3)作為開孔劑,所述聚環氧丙烧的名義羥基 官能度為1,重均分子量為8〇〇-8,50〇 g/mol。 71_如申請專利範圍第%項所示的方法,其中所述催化劑(c)為 選自下列至少一種與有機金屬催化劑的混合物:布忍司特酸 與驗金屬的鹽類或布忍司特酸與鹼土金屬的鹽類。 72. 如申凊專利範圍第71項所示的方法,其中所述布忍司特酸 0 與鹼金屬的鹽類為碳酸氫鈉。 73. 如申睛專利範圍第71項所示的方法,其中所述布忍司特酸 與鹼金屬的鹽類為碳酸鈉。 74· 士申叫專利範圍第38項所示的方法,其中所述交聯劑為如 下式所式之化合物 、 H(3x)-N-[(CH2)2-〇H]x 其令X為1、2或3的整數。 75·ίΪΐ專利範圍第74項所示的方法,其中所述交聯劑為二 項t ίϊί ί物包含以申請專利範圍第’75項中任- 48 20103700065. The method of claim 38, wherein the crosslinking agent has a weight average molecular weight of 60 to 420 g/mol and has at least two isocyanate reactive functional groups; 66. The method of the invention, wherein the crosslinking agent is used in an amount of 0.2-15 parts by weight 'mixed with 100 parts by weight of the isocyanate active 67. The method shown in claim 66 of the patent scope, Wherein the crosslinking agent is in an amount of from 1.2 to 12 parts by weight 'α 100 parts by weight of the isocyanate-containing active mixture. 6^ The wire shown in claim 38 of the patent, wherein the isocyanic surface living knife further comprises a polymer of 〇4 〇 by weight (based on 1 〇〇 part by weight of the active vinegar active component) The polyol, the polymer polyol in parts by weight, is 10. In terms of parts by weight of the polymer polyol, the method of the solid value of 22 KOH/g is as shown in item 38, and the isocyanate vinegar is 30-5.0 parts by weight (in 100 parts by weight of the foam) The total weight is 5%, and the weight average molecular weight is 800-8,500 g/md. 47 201037000 70. The method of claim 69, wherein the isocyanate-reactive component further comprises 〇_3 5 parts by weight (based on the total weight of the foam) - polyepoxy Propylene (b3) is used as a cell opener, and the polyglycidil has a nominal hydroxyl functionality of 1, and a weight average molecular weight of 8 〇〇-8, 50 〇g/mol. 71. The method of claim 5, wherein the catalyst (c) is a mixture of at least one selected from the group consisting of an organometallic catalyst: bromide acid and a metal salt or bromide acid A salt of an alkaline earth metal. 72. The method of claim 71, wherein the salt of bromide acid 0 and an alkali metal is sodium hydrogencarbonate. 73. The method of claim 71, wherein the salt of bromide acid and an alkali metal is sodium carbonate. 74. The method of claim 38, wherein the crosslinking agent is a compound of the formula: H(3x)-N-[(CH2)2-〇H]x, wherein X is An integer of 1, 2 or 3. 75. The method of claim 74, wherein the cross-linking agent is a two-item t ίϊί ί Included in the '75 patent application scope - 48 201037000 四、指定代表圖: (一) 本案指定代表圖為:第( )圖。 (二) 本代表圖之元件符號簡單說明: 無 五、本案若有化學式時,請揭示最能顯示發明特徵的化學式:4. Designation of representative drawings: (1) The representative representative of the case is: ( ). (2) A brief description of the symbol of the representative figure: None 5. If there is a chemical formula in this case, please disclose the chemical formula that best shows the characteristics of the invention:
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