TW311920B - - Google Patents

Download PDF

Info

Publication number
TW311920B
TW311920B TW83107042A TW83107042A TW311920B TW 311920 B TW311920 B TW 311920B TW 83107042 A TW83107042 A TW 83107042A TW 83107042 A TW83107042 A TW 83107042A TW 311920 B TW311920 B TW 311920B
Authority
TW
Taiwan
Prior art keywords
patent application
foam
polyol
item
compounds
Prior art date
Application number
TW83107042A
Other languages
Chinese (zh)
Original Assignee
Takeda Pharm Industry Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Takeda Pharm Industry Co Ltd filed Critical Takeda Pharm Industry Co Ltd
Application granted granted Critical
Publication of TW311920B publication Critical patent/TW311920B/zh

Links

Landscapes

  • Polyurethanes Or Polyureas (AREA)

Description

A7 311920 B7 五、發明説明() 3 〔發明範畴〕 (請先閲讀背面之注意事項再填寫本頁) 本發明偽有關於一種可用作産製硬質聚胺基甲酸酯發 泡體時當作多元醇之環氧烷與N -胺基乙基六氫吡阱之加成 物以及一種使用此加成物當作部份多元醇成份之硬質聚胺 基甲酸酯發泡體之製法。本發明尤其有關於如此之新穎加 成物和使用此加成物當作部份之多元醇成份和另外之氛氟 碩化合物當作發泡劑取代傳統之氛氣硪化合物(CFC's)之 具有高抗熱性和其他改良性質之硬質聚胺基甲酸酯發泡體 之製法。 〔先前技藝之說明〕 硬質聚胺基甲酸酯發泡體具有高熱絶綠性且亦具有優 越之模製性和加工性,所以其被廣用於冷凍裝置,建築物 ,低溫.倉庫,儲槽,冷凍船或管件當作熱絶緣物質。 經濟部中央標準局負工消費合作社印敢 産製硬質聚胺基甲酸酯發泡體時,通常使用一步方法 ,其中將主要由多元醇,催化劑,泡沫安定劑和發泡劑所 組成之A成份與主要由有機多異氰酸酯所組成之B成份一起 混合而使各成份相互反應以同時進行發泡程序和固化程序 而形成發泡體。 硬質聚胺基甲酸酯發泡體産製之發泡劑之中,常用者 為三氣氣甲烷或R-11,因為水與有機多異氰酸酯反應産十 二氣化磺氣體,所以水亦用作與R - 1 1共用之化學發泡劑。 以R-11為例之傳統氣氣碳化合物具化學安定性,因此其擴 散入同溫層而破壊臭氣層。其結果,太陽紫外線不被臭氣 層所吸收而到逹地球表面,引起全球環境問題。因此.ΓΙ 3 本紙張尺度適用中國國家橾隼(CNS ) A4規格(210X 297公釐)A7 311920 B7 V. Description of the invention () 3 [Scope of invention] (Please read the precautions on the back before filling in this page) This invention is about a kind of rigid polyurethane foam that can be used to produce Adduct of polyalkylene oxide as a polyol and N-aminoethyl hexahydropyridine trap and a method for producing rigid polyurethane foam using the adduct as a part of polyol component . The present invention is particularly concerned with the novel adducts and the use of the adducts as part of the polyol component and the addition of fluorocarbon compounds as blowing agents to replace traditional fluorocarbon compounds (CFC's). Method for preparing hard polyurethane foam with heat resistance and other improved properties. [Explanation of prior art] The rigid polyurethane foam has high thermal insulation and greenness, and also has excellent moldability and processability, so it is widely used in refrigeration equipment, buildings, low temperature, warehouses, storage Tanks, freezing ships or pipe fittings are used as thermal insulation materials. In the production of rigid polyurethane foams by Yingan, a consumer labor cooperative of the Central Standards Bureau of the Ministry of Economic Affairs, a one-step method is usually used, which will consist of polyols, catalysts, foam stabilizers and foaming agents. The components are mixed with the B component mainly composed of organic polyisocyanate to make each component react with each other to simultaneously perform a foaming process and a curing process to form a foam. Among the blowing agents produced by rigid polyurethane foams, the most commonly used is three-gas methane or R-11. Because water reacts with organic polyisocyanates to produce twelve-gas sulfonate gas, water is also used Used as a chemical blowing agent with R-11. The traditional gas-carbon compound taking R-11 as an example is chemically stable, so it diffuses into the stratosphere and breaks the odorous gas layer. As a result, solar ultraviolet rays are not absorbed by the odorous layer and reach the surface of the earth, causing global environmental problems. Therefore. ΓΙ 3 This paper scale is suitable for China National Falcon (CNS) A4 specification (210X 297mm)

311S20 經濟部中央標準局員工消費合作社印製 五、, 發明説明(4 ) 1 I 從 1989以來氧氣磺化合物之使用 已 被 禁 止 或 限 制 使 用 > 生 1 1 産 聚 胺 基 甲 酸 酯 發 泡 體 所 用 之 R - 11亦被禁 止 或 限 制 0 I I 在 這 種 情 況 下 負 取 近 許 多 研 究 人 員 已 深 入 研 究 期 能 發 产~、 請 先 閱 讀 1 1 現 可 取 代 傳 统 氯 氟 碩 化 合 物 或 另 外 之 氯 氟 碩 化 物 之 發 泡 1 1 劑 0 某些研嘴灰、員建議使用水當 作 唯 —- 之 發 泡 劑 以 取 代 R - 背 & 之 1 1 I 1 1 〇 然 而 , % 使 用 水 當 作 唯 *—* 發 泡 劑 所 産 製 之 聚 胺 基 甲 酸 注 意 事 I ] I 酯 發 泡 體 微 胞 中 僅 含 二 氣 化 磺 氣 體 > 且 因 而 發 泡 體 具 不 良 項 再 填 裝 I 之 熱 絶 緣 性 〇 另 者 9 二 氧 化 碩 氣 sm 塍 經 由 發 泡 體 之 胞 壁 擴 散 本 頁 而 由 徹 胞 漏 掉 且 撤 胞 之 内 壓 經 時 降 低 所 以 發 泡 體 體 積 收 縮 V, 1 1 | 0 在 某 程 度 上 可 同 ^xac. 思 增 加 發 泡 體 之 密 度 以 解 決 此 問 題 * 1 1 | 然 而 其 φ iiSLa 非 —- 令 人 滿 意 之 解 決 方 案 〇 1 ί 訂 1 另 一 方 面 9 例 如 二 氯 三 氣 乙 烷 (HCFC- 1 2 3 )或 二 氯 氣 乙 烷 (HCFC - 141b)之氫化氣氟磺化合物最近經發展為傳統氣 I 1 氟 碩 化 合 物 之 取 代 物 0 這 取 代 物 或 氫 化 氮 氟 磺 化 合 物 對 1 [ 臭 氣 層 較 不 具 破 壞 性 9 然 而 ί 當 考 慮 其 主 母 性 時 9 似 乎 幾 乎 L 不 可 能 將 * 刖 者 予 以 實 際 使 用 1 且 僅 後 者 可 能 可 實 際 使 用 0 1 | 然 而 > R - 11具有 23 υ 之 .Vfft 沸 點 而 HCFC -141b具有32¾之 1 1 沸 點 f 因 而 此 兩 發 泡 劑 之 沸 點 相 差 很 大 0 另 外 , HCFC 两 1 1 141b對用 於 生 産 硬 質 聚 胺 基 甲 酸 酯 發 泡 體 之 有 機 多 異 % 酸 1 1 酯 或 多 元 醇 以 及 最 終 之 聚 胺 基 甲 酸 酯 發 泡 具 有 較 大 之 溶 解 1 | 性 I 使 用 HCFC -141b當作發泡劑之硬質聚胺基甲酸酯發泡 1 1 體 之 製 造 較 使 用 傳 統 R - 11當作發泡劑製得 之 硬 質 發 泡 體 伴 1 1 I 隨 産 生 之 例 如 較 低 流 動 性 和 較 低 之 發 泡 體 尺 寸 準 確 性 之 問 1 I 1 題 0 同 時 1 由 加 工 經 濟 之 觀 因為HCFC -1 4 1 b之價格昂貴 1 1 本纸張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 4 (修正頁) 經濟部中央梂準局負工消費合作杜印策 A7 B7 五、發明説明() 5 以及由環境保護之觀點,期望降低使用HCFC-14U當作發 泡劑之用量。 〔發明概述〕 因此本發明之目的傜為了解決上述之問題且提供一種 可用於硬質聚胺基甲酸酯發泡體之製造時用作多元醇之瑞 氧烷與N -胺基乙基六氫吡畊之新穎加成物和提供一種使用 此加成物當作部份所用之多元醇成扮之硬質聚胺基甲酸酯 發泡體之製法。 本發明之特定目的傜提供一種硬質聚胺基甲酸酯發泡 體之製法,該發泡體具有高抗熱性和高尺寸安定性,藉使 用如上述之加成物當作部份所用之多元醇成份和使用宜以 較少量之另外氯氣碩化合物和水之混合物之當作發泡劑之 另外氣氣碩化合物以取代以R - 11為例之傳統氣氣碩化合物 以改良發泡效率之其他改良性質。 本發明提供一種具有下式之環氧烷與N -胺基乙基六氫 吡阱之加成物 % /\ >·(Ε0) - (Ρ0) 一 Η Η-(ΡΟ) -(ΕΟ) -Ν N-CH0CH_N^ n1 m1311S20 Printed by the Employee Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economy V. Description of the invention (4) 1 I The use of oxygen sulfonate compounds has been prohibited or restricted since 1989 > Health 1 1 Polyurethane foam produced The R-11 used is also forbidden or restricted. 0 II In this case, the negative value is near. Many researchers have already produced in-depth research period. Please read first. 1 1 can now replace traditional chlorofluorocarbon compounds or other chlorofluorocarbons The foaming of the master chemical 1 1 agent 0 Some researchers have suggested using water as the only blowing agent instead of R-back 1 1 I 1 1 〇 However,% uses water as the only * — * Cautions for Polyurethane Produced by Foaming Agent I] I ester foam cells contain only digasified sulfonate gas>, and thus the foam has defective items and the thermal insulation of I 〇Another 9 Smok dioxide diffused through the cell wall of the foam body Leakage and the internal pressure of the cell removal decrease with time, so the foam volume shrinkage V, 1 1 | 0 can be the same as ^ xac. Consider increasing the density of the foam to solve this problem * 1 1 | However, its φ iiSLa Non--satisfactory solution 〇1 ί Order 1 On the other hand 9 Hydrogenated fluorosulfon compounds such as dichlorotriethane (HCFC- 1 2 3) or dichloroethane (HCFC-141b) Developed as a substitute for the traditional gas I 1 fluorocarbon compound 0 This substitute or hydrazine fluorosulfonate compound 1 [The odor layer is less destructive 9 However, when considering its main motherhood 9 seems to be almost L impossible. * The actual use is 1 and only the latter may be actually used 0 1 | However > R-11 has a boiling point of 23 V. Vfft and HCFC-141b has a boiling point f of 32¾ of 1 1 so the boiling points of the two blowing agents are very different Big 0 In addition, HCFC two 1 1 141b is used to produce rigid polyurethane Organic polyiso% of ester foams 1 1 Ester or polyol and the final polyurethane foam has greater dissolution 1 | Property I Hard polyamine groups using HCFC -141b as blowing agent The production of formate foam 1 1 body is more rigid than traditional R-11 used as a foaming agent with 1 1 I. For example, the resulting lower fluidity and lower foam size accuracy Question 1 I 1 Question 0 At the same time 1 From the perspective of processing economy Because the price of HCFC -1 4 1 b is expensive 1 1 This paper scale is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm) 4 (Amendment page) Economy The Ministry of Central Bureau of Pre-Examination and Duty Consumption Cooperation Du Yince A7 B7 Fifth, the invention description () 5 and from the perspective of environmental protection, I hope to reduce the amount of HCFC-14U used as a blowing agent. [Summary of the Invention] Therefore, the purpose of the present invention is to solve the above-mentioned problems and to provide a reoxyxane and N-aminoethylhexahydrogen which can be used as polyols in the manufacture of rigid polyurethane foam The novel adducts of pyrigallium and a method for providing a rigid polyurethane foam using the polyol used as part of this adduct. The specific object of the present invention is to provide a method for producing rigid polyurethane foam, which has high heat resistance and high dimensional stability, and uses the above-mentioned adducts as part of the multi-component Alcohol composition and use should use a smaller amount of a mixture of another chlorine gas master compound and water as a foaming agent to replace the traditional gas gas master compound with R-11 as an example to improve the foaming efficiency. Other improved properties. The present invention provides an adduct of alkylene oxide and N-aminoethyl hexahydropyridine trap with the following formula% / \ > · (Ε0)-(Ρ0) -Η Η- (ΡΟ)-(ΕΟ) -Ν N-CH0CH_N ^ n1 m1

3 3 \—/ \(E0) - (PO) -H n2 m2 其中EO為氣伸乙基;PO為氣伸丙基;ηι, Π2和H3為氣伸乙 基之平均數目;111+112 + 113 = 2.0-3.5: mi, ra'2和m3為氣(申丙 基之平均數目;且 πιι+πΐ2 + ιη·3 = 3.0-6.0。 (請先閲讀背面之注意事項再填寫本頁} 7 -裝-- --訂 I nn HH I — nn nn m^i I-In nn · 本紙張尺度適用中國國家標準(CNS ) A4见格(210X297公釐) 5 A7 311820 B7 五、發明説明() 6 〔圖示之簡要說明〕 第1圓為本發明加成物之一實施例之多元醇A之紅外線 吸收光譜; 第2圖為多元醇A之質子核磁共振光譜; 第3圖為多元醇A之三氣乙醯化産物之質子核磁共振光 譜。 第4圖顯示在實施例I,比較例I和II中HCFC-141b之用 量與最終發泡體之密度的關偽;以及 第5圖顯示在實施例II和比較例III中HCFC-141b用量 和最終發泡體密度之關偽。 〔發明之詳細說明〕 已知者為可藉添加環氧烷至在分子上具有活性氫之當 作起始劑之化合物製造一加成物,藉此提供一種環氣烷之 加成物。 環氣烷與胺基乙基六氫吡阱之加成物可依相同方式 製得。因此,其僳藉首先添加2.0-3.5莫耳φ之環氣乙烷 至1莫耳份之Ν -胺基乙基六氫吡阱,藉此形成一般式(I)中 以Ε0表示之氣伸乙基,其中添加至Ν -胺基乙基六氫吡畊之 璟氣乙烷之平均數目傜以Π2和Π3表示,且其次添加 3.0-6.0莫耳份之環氣丙烷至1莫耳份之最终的與N -胺基乙 基六氫吡畊所形成之環氣乙烷加成物,葙此形成一般式( ί)中以P0所表示之氣伸丙基,基中添加至N -胺基乙基六氣 吡肼之環氣丙烷之平均數目偽以ai, η 2.和ra 3表示者u _更詳細的説,預定量之環氣乙烷首先在1 〇 〇 -〖2 0 f之 i紙f尺度適用中ϋΐ#準(CNS ) A4規格(210X297公廣) (請先閲讀背面之注意事項再填寫本頁) 經濟部t央梂隼局負工消費合作社印製3 3 \ — / \ (E0)-(PO) -H n2 m2 where EO is air-extended ethyl; PO is air-extended propyl; ηι, Π2 and H3 are the average number of air-extended ethyl; 111 + 112 + 113 = 2.0-3.5: mi, ra'2 and m3 are gas (the average number of propyl groups; and πι + πΐ2 + ιη · 3 = 3.0-6.0. (Please read the precautions on the back before filling out this page) 7-Install ---Subscribe I nn HH I — nn nn m ^ i I-In nn · The paper size is applicable to China National Standard (CNS) A4 see grid (210X297mm) 5 A7 311820 B7 5. Description of invention () 6 〔 Brief Description of the Figure] Circle 1 is the infrared absorption spectrum of Polyol A which is an embodiment of the adduct of the present invention; Figure 2 is the proton nuclear magnetic resonance spectrum of Polyol A; Figure 3 is Polyol A III The proton nuclear magnetic resonance spectrum of the gas acetylation product. Figure 4 shows the relationship between the amount of HCFC-141b and the density of the final foam in Example I, Comparative Examples I and II; and Figure 5 shows in the example The relationship between the amount of HCFC-141b and the density of the final foam in II and Comparative Example III. [Detailed description of the invention] It is known that by adding alkylene oxide to have active hydrogen on the molecule The compound used as the starting agent makes an adduct, thereby providing an adduct of cycloalkane. The adduct of cycloalkane and aminoethylhexahydropyridine trap can be prepared in the same way. , By first adding 2.0-3.5 mole φ of ring gas ethane to 1 mole of N-aminoethyl hexahydropyridine trap, thereby forming the gas-extended ethylene represented by E0 in the general formula (I) The average number of Jing gas ethane added to N-aminoethyl hexahydropyrrolidine is represented by Π2 and Π3, and then 3.0-6.0 mole parts of cyclopropane is added to the final of 1 mole part The cyclic gas ethane adduct formed with N-aminoethyl hexahydropyridinium, which forms the gas-propyl group represented by P0 in the general formula (ί), and the group is added to the N-amino group The average number of ring gas propane of ethyl hexahydropyrazine is pseudo-represented by ai, η 2. and ra 3 u _ More specifically, the predetermined amount of ring gas ethane is first in the range of 1 〇〇- 〖2 0 f The i paper f scale is applicable to the standard (CNS) A4 specification (210X297 public broadcasting) (please read the precautions on the back and then fill out this page) Printed by the Ministry of Economic Affairs, Tung Kang Falcon, Unemployed Consumer Cooperative

6 經濟部中央標準局員工消費合作社印製 —修正 年月日 、A7 _ 補充_ 五、發明説明(7 ) 溫度下與N -胺基乙基六氫吡阱反應。反應係在無催化劑存 在下進行,然而,必要時亦可使用催化劑。在璟氣乙烷反 應完成之後,然後在以最終加成産物之重量為基準之0. ΙΟ.4 重量 $ 之量的 當作催 化劑之 於燒瓶 中之氫 氧化鉀 存在下 ,於100-120Ό之溫度下使預定量之環氧丙烷與環氣乙烷 加成步驟之所得産物反應。將與Μ -胺基乙基六氫吡畊反應 之環氧乙烷和環氣丙烷之量像視最終加成産物之分子量或 羥值,或與Ν -胺基乙基六氫吡阱之目標氧伸乙基/氣伸丙 基加成物而定。 依序之環氣乙烷和環氣丙烷加成反應之後,反應産物 以例如草酸,稀硫酸或磷酸之酸,或以例如合成矽酸_之 鹼吸附劑處理以便使反應産物中之氫氣化鉀去活性。然後 以過濾作用移除固態物質且藉置反應産物於減壓下或將惰 性氣體吹入反應産物而由反應産物中移除水。通常宜使反 應産物脱水至少於0.10¾之水含量。通常像添加至少約500 ppm至ΙΟΟΟΡΡΒ之BHT(2,6-二第三丁基-4-甲酣)至加成物予 以安定化處理。 本發明進一步提供一種包括在發泡劑之存在下使有機 多異氡酸酯成份與多元酯反應之硬質聚胺基甲酸酯發泡體 之製法,其中多元醇成份包括本文上述之加成物。 如示於卩.纟.(:11「「丨6「之美國專利第3,251,788號所熟 知之在發泡劑之存在下,有機多異氰酸酯成份與含有當作 部份多元醇成份之環氣丙烷與N -胺基乙基六氫吡畊之加成 物之多元醇成份反應以製造硬質聚胺基甲酸酯發泡體。 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公嫠) 7 (修正頁) ---------f 裝------訂 ^ 4^ (請先閲讀背面之注意事項再填寫本頁) 311920 卜 η’ :':一Ί_I热物補充I $_五、發明説明(8 ) 然而,本發明使用依序環氣乙烷與環氧丙烷與Η -胺基 經濟部中央標準局員工消費合作社印製 環發合合度 醇物所 寸另氟環亦性 莫 之力 於 之善化混密 元成下 尺於氯之法工 每爿份貞 低 知改碩之低 多加件。高可外畊方加 於#0耳 ^ 量 熟著氤水有 之之條性和體另吡本或 少1ί莫 i 烷 獲 之 代顯氯與具 份畊溫定性泡少氫。性 量自每纟 丙 法 物 取現之物得 部吡高安綠發減六率製 之_ 過双 氣 份發外合獲 作氫和寸絶酯可基效模 烷 超 Λ。 環 成已另化而 當六濕尺熱酸因乙泡之 乙 ta#/J體之 醇物和碳 , 物基在之善甲用基發越 氣❾之ττί泡肼 元成物氣物 成乙使善改基合胺i 優 環 Ϊ 烷卩發吡 I 耳 , 多加成氛合 加基即改有胺水 N 改得 之 — 乙 Ϊ 質氫 ^時 之之加外化 明胺而有具聚與與得獲 畊 ο 氣 硬六 份畊 明另碩 。發N-因具 ,質宜 之獲可 吡2.環 f 之.基 耳 部吡發之氣體本與 ,體法硬 ,序而中 氫阱之 度乙 作氫本量氛泡用烷應泡方之下依物其 六吡加 5' 強基 當六用減統發使丙反發明質在用成 , 基氫添3.夠胺 物 基使以傳酯為氣制酯 發性存使加法 乙六而畊足H-成乙藉宜之酸點環控酸本善之藉烷泡 基基 ,吡有至 加基 , ,11甲優之易甲之改物 ,丙發 胺乙率氫具加 畊胺者劑R-基之知容基示他合量氧佈H-基效 六造當 吡N-另泡如胺步熟較胺所其化之環噴 至胺泡基製 , 氫與 。發例聚一 代能聚上和磺物和於 加H-發乙法著 六 烷率作代質進取可質如性氟合烷用 當之之基無接 基丙效當取硬 份得硬 定氛化乙應 份良胺而 乙氣泡物物之 成使得 安外碩 氣可。 耳改N-低 (請先閲讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 8 (修正頁) 释修正 A7 B7 經濟部中央標準局員工消費合作社印製 WX: 五、發明説明(9 ) 每 莫 耳 份 之 N - 胺 基 乙 基 -JU. 氫 吡 阱 3 , 0莫耳份時, 0 〒得加成 物 具 有 許 多 在 分 子 末 端 之 殘 留 胺 基 和第一级羥 基 f 所以反 應 難 以 控 制 > 但 當 噴 佈 發 泡 進 行 時 ,所得硬質 發 泡 體亦可 發 生 層 分 離 0 焦 化 亦 可 能 發 生 0 當 所添加之璟 氧 丙 烷量超 過 每 莫 耳 份 之 Η - 胺 基 乙 基 氫 吡 畊 6 . 0莫耳份, 所得加成 物 之 羥 值 太 低 而 無 法 製 造 具 有 足 夠 強度之硬質 發 泡 la 〇 - 本 發 明 所 用 之 較 宜 加 成 物 為 例 如藉首先添 加 2 . 5-3.0 莫 耳 份 之 環 氧 乙 院 至 1莫耳 份之N -胺基乙基六氫吡畊,且 然 後 添 加 3 . 5- 6 . 0莫耳份之環氧丙烷至1莫耳份 之 N - 胺基乙 基 氫 吡 畊 而 製 得 0 以 結 構 為 基 準 > 亦 即 添 加 至 N - 胺基乙基六 氫 吡 畊之環 氧 乙 烷 和 環 氧 丙 烷 之 量 9 加 成 物 具 有不超過430mgK0H/g之 羥 值 〇 然 後 9 加 成 物 宜 具 有 不 低於 3 0 0 mgi(0H/g之 羥 值。羥 值 為300至430 m g Κ0Η/ g之範 圍之加成物具有35 0至 561之範 圍 之 平 均 分 子 量 〇 當 加 成物具有小於3 0 0 π g K 0 H / g之羥值時 9 可 能 常 常 不 易 製 造 具 有 足 夠 強 度 乏硬質聚胺 基 甲 酸酯發 泡 體 〇 更 宜 使 用 所 用 多 元 醇 成 份 之 1 0 -40重量尤之 量 的 加成物 Ο 當 多 元醇成份含有低於ίο重悬之量的加成物時, 常常 不 易 製 得 具 有 如 本 文 前 述 之 許 多 方 面上之改良 性 質 之硬質 聚 胺 基 甲 酸 酯 發 泡 體 > 而 i 多 元 醇 成份含有超 過 40重量S; 之 量 的 加 成 物 時 > 則 常 常 不 易 控 制 反應。 本 發 明 所 用 多 元 醇 成 份 含 有 當 作第一多元 醇 之 加成物 和 第 二 多 元 醇 〇 任 何 非 加 成 物 之 多 元醇可用作 第 二 多元醇 ---------^种衣— (請先鬩讀背面之注意事項再填寫本頁) 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 9 (修正頁)6 Printed by the Employee Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs-Amendment Date, A7 _ Supplement _ V. Description of invention (7) Reacts with N-aminoethylhexahydropyridine trap at temperature. The reaction is carried out in the absence of a catalyst, however, a catalyst can also be used if necessary. After the Jing gas ethane reaction is completed, then in the presence of potassium hydroxide in the flask in the amount of 0. ΙΟ.4 weight $ based on the weight of the final addition product as a catalyst, in the range of 100-120Ό At a temperature, a predetermined amount of propylene oxide is reacted with the product obtained in the ring gas ethane addition step. The amount of ethylene oxide and cyclopropane reacted with M-aminoethylhexahydropyridine depends on the molecular weight or hydroxyl value of the final addition product, or the target with N-aminoethylhexahydropyridine trap Oxygen extended ethyl / gas extended propyl adduct. After the sequential addition reaction of ring gas ethane and ring gas propane, the reaction product is treated with an acid such as oxalic acid, dilute sulfuric acid or phosphoric acid, or with an alkaline adsorbent such as synthetic silicic acid to make potassium hydrogen in the reaction product Deactivated. Then, the solid matter is removed by filtration and water is removed from the reaction product by using the reaction product under reduced pressure or blowing an inert gas into the reaction product. It is generally advisable to dehydrate the reaction product to a water content of at least 0.10¾. Generally, it is like adding at least about 500 ppm to 100 ppm BHT (2,6-di-third-butyl-4-methylpyridine) to the adduct to stabilize it. The present invention further provides a method for producing a rigid polyurethane foam comprising reacting an organic polyisodonate component with a polyhydric ester in the presence of a foaming agent, wherein the polyhydric alcohol component includes the adducts described above . As shown in 卩. 纟. (: 11 "" 丨 6 "of US Patent No. 3,251,788 is well known in the presence of a blowing agent, the organic polyisocyanate component and the content of polyhydric alcohol component containing cyclopropane and The polyol component of N-aminoethylhexahydropyrrolidine adduct reacts to produce rigid polyurethane foam. This paper scale is applicable to China National Standard (CNS) A4 specification (210X297 public daughter) 7 (Corrected page) --------- f Installed ------ ordered ^ 4 ^ (Please read the notes on the back before filling in this page) 311920 bu η: :: a Ί_I hot object supplement I $ _V. Description of the invention (8) However, the present invention uses the ring gas ethane and propylene oxide in sequence with the H-amino based employee consumer cooperative of the Central Standards Bureau of the Ministry of Economic Affairs to print the ring compound alcohol. There is no difference in the ability to improve the mixed cipher Yuan into a low-level add-on piece for the magician of chlorine. Each piece of the virginity is changed from the low to the knowledge. The high can be cultivated in the field # 0 耳 ^ Amount of cooked water Some of the characteristics are different from those of pyribene or less than 1 mol. It is obtained by replacing chlorine and qualitatively cultivating temperature, and qualitatively absorbing less hydrogen. It is a system of reducing the ratio of six of Pygolol green hair to _ over two gas fractions, which can be used as hydrogen and an ester to form an effective super-alkane. Alcohols and carbon of the etha # / J body, the base is good, and the base is used to make the gas ❾ of the ττί hydrazine element. Ear, multi-addition atmosphere addition base is changed to amine water N to get it-ethyl hydrogen hydrogen ^ when the addition of externalized amine, and has the ability to get together with the gas hard six gas cultivating another. N-due to the quality, the quality can be obtained. 2. The gas of the ring f. The gas in the base of the ear is inherently hard, the method is hard, and the order of the hydrogen trap is hydrogen. Under the formula, its hexapyridine is added to the 5 'strong base. When the six-use reduction system is used, the anti-inventive substance is in use. The base hydrogen is added to 3. The amine compound makes the ester transfer as a gas-based ester. B-six cultivating enough H-to-B by suitable acid point cyclic control acid goodness by alkanoyl group, pyridyl to glyceryl,, 11 A excellent and easy to change the modified product, promethamine ethyl hydrogen rate plus The knowledge of R-based cultivator's agent R-base shows the amount of oxygen cloth H- The basic effect is six-fold, when the pyridine N-another foam, such as the amine step is more mature than the amine, the ring is sprayed to the amine foam base system, hydrogen and hydrogen. In the case of the first generation, it can be polymerized with sulfide and added with H-fat method. Hexane rate is used as a substitute for quality, and it can be used as a suitable fluoroalkane. It is based on a non-linked base. When it is hard, it can be hardened to obtain a hard amine. Yes. Ear change N-low (please read the precautions on the back before filling in this page) This paper size is applicable to China National Standard (CNS) A4 specification (210X297mm) 8 (Amendment page) Amendment A7 B7 Central Standards of Ministry of Economic Affairs WX printed by the Bureau ’s Consumer Cooperatives: V. Description of the invention (9) N-aminoethyl-JU per mole fraction. When the hydrogen pyridine trap is 3, 0 mole fractions, 0 〒 the adduct has many in-molecules. The residual amine group at the end and the first-stage hydroxyl group f make the reaction difficult to control. However, when spray foaming is performed, the resulting rigid foam can also undergo layer separation. 0 Coking can also occur. 0 When the amount of oxypropane added More than every Molar parts of H-aminoethylhydropyrrolene 6.0 molar parts, the hydroxyl value of the resulting adduct is too low to produce a hard foam with sufficient strength la 〇- The present invention is more suitable for addition The substance is, for example, by first adding 2.5-3.0 mol parts of ethylene oxide to 1 mol part of N-aminoethyl hexahydropyrazine, and then adding 3.5-6.0 mol parts Propylene oxide to 1 mole part of N-aminoethylhydropyrrolidone is prepared to 0 based on the structure> that is, ethylene oxide and epoxy added to N-aminoethylhexahydropyrrolidone The amount of propane 9 adduct has a hydroxyl value of not more than 430 mgKOH / g. Then the 9 adduct preferably has a hydroxyl value of not less than 300 mgi (0H / g. Adducts with a hydroxyl value in the range of 300 to 430 mg Κ0Η / g have an average molecular weight in the range of 35 0 to 561. When the adduct has a hydroxyl value of less than 3 0 0 π g K 0 H / g 9 may often It is not easy to make a rigid polyurethane foam with sufficient strength. It is more suitable to use the adducts in an amount of 1-40 weight percent of the polyol component used. When the polyol component contains less than ίο resuspended amount When it is adducts, it is often not easy to produce rigid polyurethane foams with improved properties in many aspects as mentioned above, and the polyhydric alcohol component contains more than 40 weight S; In the case of > it is often difficult to control the reaction. The polyol component used in the present invention contains an adduct of the first polyol and a second polyol. Any non-adduct polyol can be used as the second polyol --------- ^ Seeds— (please read the precautions on the back before filling out this page) This paper size is applicable to China National Standard (CNS) A4 specification (210X297mm) 9 (Amendment page)

'1T'1T

經濟部中央梂準局貝工消費合作杜印5L A7 B7 五、發明説明() 10 ,然而,第二多元醇具有當多元醇全量使用時羥值為300 至7 0 0 mgKOH/g範圍之羥值。當多元醇成份具有小於3 0 0 π!κ Κ0Η“之羥值時,常常不易製得具有足夠強度之硬質聚胺 基甲酸酯發泡體。當多元醇成份具有超過7 0 0 mgK0H/s之經 值時,常常發生所得硬質聚胺基甲酸酯發泡體太脆且黏著 強度亦不良之情形。 第二多元醇因此宜為一種藉添加例如環氣乙烷,環氣 丙烷,環氣丁烷或這些之混合物等之環氧烷至分子上具有 活性氫之有機化合物而製得之多醚多元醇且此第二多元醇 具有300-300ngK0H/g之範圍之羥值。在分子上具有活性氫 之有機物可為例如甘油,三(羥甲基)丙烷,季戊四醇,一 縮二甘油,甲基葡糖苷,山梨糖醇或蔗糖等之多元醇,·例 如乙二胺之脂族多官能胺;例如鄰間-或對-甲代苯撑 二胺之芳族多官能胺;或例如三(羥乙基)胺之烷醇胺。 本發明所用之有機多異氡酸酯成分宜為芳族多異氡酸 酯。芳族多異氡酸酯没有特別限制,然而,較宜者為多伸 甲基多苯基多異氛酸酯,亦稱為粗MDI, C-MDI或聚合物 MDI,粗甲代苯撑二異氣酸酯(TDI), TDI -預聚物或這些之 混合物。最宜者為含有不少於70重量χ之量的多伸甲基多 苯基多異氰酸酯之粗MDI。 粗 MDI可以例如 Luplanate M20S或 Luplanate M-12S( T a k e d a Bad i s c h e Urethane Kogyo K. K. ) , P A P l - 1 3 5 ( Mitsubishi 化學 Dow), Sumidur 44V-20或 44V-l〇( Sumitomo Bayer.)或 Millionate MR-100 或 Millionat。 本紙張尺·度適用中國國家標率(CNS ) A4現格(210X297公釐) 1 〇 1-^- it I -- ΙΪ (請先閱讀背面之注意事項再填寫本頁) T n I n 、—=° 線-- -flflu —^m ^nfl : 經濟部中央標隼局負工消費合作杜印製 A7 B7 五、發明説明() 11 MR-200(Nippon Polyurethane K. K.)等供應。 有機多異氟酸酯成份僳在85-150之^異氰酸酯指數下與 多元醇成份反應。異氮酸酯指數定義為[真正所用多異氰 酸酯之量/計算所得需要與羥基化合物(多元醇)之活性氫 和若存在任何之水反應之多異氣酸酯之量]xlOO之值。使 用少於85異氣酸酯指數不易形成具有不良尺寸安定性之硬 質聚胺基甲酸酯發泡體,而使用超過150異氡酸酯指數不 易獲得其内焦化或脆化之發泡體。 本發明以卜11為例之傳統氣氟碩化合物之其他物和取-代物為氫化氨氟碩化合物或宜為1至2個碩之烷,氫化氟硪 化合物或宜為2至4個碩之烷或金氟碩化合物或宜為4至6個 碩之烷而其中所有之氫皆被氤原子所取代。這些化合物廳 具有低沸點,亦即可揮發性。 因此,此取代物之實例可為例如HCFC-141b, HCFC-123(1,卜二氣-2,2 ,2 -三氟乙烷,具27.5Ό之沸點), HCFC-142bU-氯- 二氣乙烷,具- 9.71C 之沸點), 5 H C F C - 2 2 (氣二氣甲烷,具-4 0 . 8 t 之沸點),H C F - 1 3 4 a (. 1 -氣-2,2,2 -三氟乙烷,具- 26.3Ό之沸點)。然而這些化合 物之中,待宜者為HCFC-141b。 亦可使用例如脂族或環脂族烴之烴,例如正戊烷,设 戊烷,異戊烷或這些之混合物。亦可使用二氣甲烷。 本發明所用取代物之量可視所欲製造之發泡體的密度 ifii輕易予以決定。例如,相對於1 0 0重量份所用之多元醉 成份之量.可通常使用10-60重量份之量的HCFC-141b, Μ 本紙浪尺度適用中國國家標準(CNS ) Α4规格(210X297公釐) ι ι (請先閱讀背面之注意事項再填寫本I) Ί 裝------訂-----(線 經濟部中央梂準局員工消費合作杜印製 A7 B7 五、發明説明() 12 如HCFC-22在正常溫度下為氣體之取代物通常可使用相對 於100重量份所使用多元醇之不超過20重量份之量。 本發明中,取代物宜與水合用。如上所述,HCFC-141b為本發明中最宜使用之發泡劑之一,然而,其較昂贵 ,所以一方面,HCFC-141b之使用量宜愈小愈好。另一方 面,當取代物與水合用時,發泡反應之進行傺藉HCFC-14 lb和二氧化碩兩種氣體去形成徹胞。發泡反應之後,在 室溫附近HCFC-14U氣體發生冷凝所以徹胞之内壓降至某 一程度,而在室溫下或甚至大大低於室溫下二氧化碳仍然 為氣體,且因而所得發泡體徹胞中之壓力降期望地受到限 制。 通常,硬質發泡體之尺寸安定性視骨幹結構和徹胞内 外壓差而定。當使傳統氣氟碩化合物之取代物與水合用作 為發泡劑,當所得發泡.體冷却至室溫附近,則僅産生較僅 使用取代物為發泡劑之發泡體為小之徹胞内外壓差,因為 當取代物冷凝後徹胞中之二氣化碩仍為氣體且因此最終發 泡體具有改善之尺寸安定性。取代物與水合用當作發泡劑 於是具有發泡體性質以及加工經濟性上之優點。 本發明之最宜具體實例中,以100重量份所用之多元 醇成份為基準,使用與1.0-3.0重童份之量的水合用之15-4 0重量份之量的H C F C - 1 4 1 b。當水量使用低於相對於1 0 0 ® 量份所用之多元醇成份之1.0重量份時.發泡效率無法權 得顯箸的改良,而當水量使用超過相對於1 0 0重量份所用 之多元醇成份之3 . 0重量份時,可能獲得因二氣化踽經由 本紙浪尺度適用中國國家標隼(CNS ) A4規格(210X 297公釐) 12 (請先閱讀背面之注意事項再填寫本頁) -裝' 訂 線 經濟部中央揉隼局具工消費合作社印製 A7 B7 五、發明説明() 13 胞壁擴散至外面之尺寸安定性的反效果。 多元醇成份與有機多異氰酸酯成份反應以製造硬質聚 胺基甲酸酯發泡體宜在催化劑或泡沫安定劑存在下進行。 所用之催化劑沒有待別限定,任何熟知之催化劑皆可使用 。較宜之催化劑為胺催化劑,包括例如四甲基己二胺( TMHDA,以 KAORIZER N0.1 供應(Kao K. K.)或 TOYOCAT-MR(Toso Κ· K.)),五甲基二伸乙基三胺(PMDETA,以 K A 0 RI Z E R H 0 . 3 供應(K a ο K . K .)或 T 0 Y 0 C A T - D T ( T 〇 s ο K · K .)),三伸乙基二胺之一縮二丙二醇溶液(通常縮寫為 TEDAL-33,以 DABC0-33LV供應(Air Products)),或雙(2-甲基胺基乙基)醚(以TOYOCAT ET供應(Toso K. K·))。催 化劑可單獨使用或以混合物使用。 以上所舉例以外之胺催化劑或必要時亦可使用有機金 S化合物當作催化劑。尤其以噴佈發泡製造硬質發泡體時 ,例如辛酸鉛和二月桂酸二丁基錫之有機金屬化合物。 催化劑通常以基於所用多元醇之0.01-5重量%之量使 t 用。 所用之泡沫安定劑亦沒有持別限定,任何泡沫安定劑 皆可使用。所用之泡沫安定劑包括例如B-8404, B-8407或 B - 8 4 2 5 (由 G 〇 1 d S c h in i d t 供應),F - 3 0 5 , F - 3 4 5 或 F - 3 7 3 (由The Ministry of Economic Affairs, Central Bureau of Industry, Beigong Consumer Cooperation Duin 5L A7 B7 V. Description of the invention () 10 However, the second polyol has a hydroxyl value range of 300 to 700 mgKOH / g when the polyol is used in full amount Hydroxyl value. When the polyol component has a hydroxyl value of less than 3 0 0 π! Κ Κ0Η ", it is often difficult to produce a rigid polyurethane foam with sufficient strength. When the polyol component has more than 70 mgK0H / s It is often the case that the resulting rigid polyurethane foam is too brittle and the adhesive strength is also poor. The second polyol is therefore preferably a kind of by adding, for example, ring gas ethane, ring gas propane, ring A polyether polyol made from alkylene oxide of butane or a mixture of these to an organic compound having active hydrogen on the molecule and this second polyol has a hydroxyl value in the range of 300-300ngKOH / g. In the molecule The organic substance with active hydrogen on it may be polyhydric alcohol such as glycerin, tris (hydroxymethyl) propane, pentaerythritol, diglycerol, methylglucoside, sorbitol or sucrose, etc. Functional amines; for example, ortho- or p-toluene diamine aromatic polyfunctional amines; or, for example, tris (hydroxyethyl) amines, alkanolamines. The organic polyisodonate component used in the present invention is preferably Aromatic polyisoradonate. Aromatic polyisoradonate is not particularly limited System, however, the more suitable is polymethyl polyphenyl polyisocyanate, also known as crude MDI, C-MDI or polymer MDI, crude tolylene diisocyanate (TDI), TDI -A prepolymer or a mixture of these. The most suitable is a crude MDI containing polymethyl polyphenyl polyisocyanate in an amount of not less than 70% by weight. The crude MDI may be, for example, Luplanate M20S or Luplanate M-12S (T akeda Bad ische Urethane Kogyo KK), PAP l-1 3 5 (Mitsubishi Chemical Dow), Sumidur 44V-20 or 44V-l〇 (Sumitomo Bayer.) Or Millionate MR-100 or Millionat. This paper ruler and degree are applicable to Chinese national standard Rate (CNS) A4 cash (210X297 mm) 1 〇1-^-it I-ΙΪ (please read the notes on the back before filling this page) T n I n, — = ° line--flflu — ^ m ^ nfl: The Ministry of Economic Affairs, Central Standard Falcon Bureau, Negative Work Consumer Cooperation, Du Printed A7 B7 V. Description of the invention () 11 MR-200 (Nippon Polyurethane KK), etc. The supply of organic polyisofluorate is 85-150 The isocyanate index reacts with the polyol component. The isocyanate index is defined as [the amount of polyisocyanate actually used per meter The resulting amount of polyisogas acid ester that needs to react with the active hydrogen of the hydroxy compound (polyol) and if any water is present] xlOO. Using less than 85 isogas ester index is not easy to form a hard with poor dimensional stability Polyurethane foams, and foams with internal scorch or embrittlement that are not easily obtained with an index of more than 150 isodonate. In the present invention, the other substances and substitutes of the conventional gas-fluoride master compounds of Bu 11 are hydrogenated ammonia-fluoride master compounds or preferably 1 to 2 master alkyls, and the hydrogenated fluoride master compounds are preferably 2 to 4 master compounds. The alkane or gold-fluoride master compound may be 4 to 6 master alkane and all the hydrogens are replaced by amber atoms. These compounds have a low boiling point, that is, they are volatile. Therefore, examples of such substitutes may be, for example, HCFC-141b, HCFC-123 (1, digas-2,2,2-trifluoroethane, with a boiling point of 27.5Ό), HCFC-142bU-chloro-digas Ethane, with a boiling point of-9.71C), 5 HCFC-2 2 (gaseous digas methane, with a boiling point of-4 0.8 t), HCF-1 3 4 a (. 1 -gas-2,2,2 -Trifluoroethane, with a boiling point of 26.3Ό). However, among these compounds, HCFC-141b is the best candidate. Hydrocarbons such as aliphatic or cycloaliphatic hydrocarbons such as n-pentane, pentane, isopentane or mixtures of these can also be used. Dichloromethane can also be used. The amount of substitute used in the present invention can be easily determined by the density ifii of the foam to be produced. For example, relative to 100 parts by weight of the amount of multi-component components used. 10-60 parts by weight of HCFC-141b can be generally used. Μ This paper wave scale is applicable to China National Standard (CNS) Α4 specifications (210X297 mm) ι ι (please read the precautions on the back before filling in this I) Ί outfit ------ ordered ----- (The Ministry of Economic Affairs, Central Bureau of Economic Development, employee cooperation cooperation printed A7 B7 V. Invention description ( ) 12 If HCFC-22 is a gas substitute at normal temperature, it can usually be used in an amount not exceeding 20 parts by weight relative to 100 parts by weight of the polyol used. In the present invention, the substitute is preferably used in combination with water. HCFC-141b is one of the most suitable blowing agents used in the present invention, however, it is more expensive, so on the one hand, the amount of HCFC-141b used should be as small as possible. On the other hand, when the substitute is used with hydration At the time, the foaming reaction proceeded through two gases, HCFC-14 lb and SiO2, to form a cell. After the foaming reaction, the HCFC-14U gas condensed near room temperature, so the internal pressure of the cell fell to a certain level. Degree, while at room temperature or even much lower than room temperature carbon dioxide is still a gas And the pressure drop of the resulting foam through the cell is desirably limited. Generally, the size stability of the rigid foam depends on the backbone structure and the pressure difference between the inside and outside of the cell. Hydration is used as a foaming agent. When the resulting foam is cooled to around room temperature, it will only produce a smaller pressure difference between the inside and outside of the foam than the foam with only the replacement as the foaming agent, because when the replacement condenses The second gasification master in the cell is still gas and therefore the final foam has improved dimensional stability. The replacement and hydration used as a foaming agent then has the advantages of foam properties and processing economy. In the most suitable specific example, based on 100 parts by weight of the polyol component used, HCFC-1 4 1 b in an amount of 15-4 0 parts by weight hydrated with 1.0-3.0 parts by weight of child parts is used. When the amount of water used is less than 1.0 part by weight of the polyol component used relative to 100 parts by weight. The foaming efficiency cannot be significantly improved, but when the amount of water used exceeds the amount of polyol used relative to 100 parts by weight. 3.0 parts by weight of ingredients Due to the two gasification standards, the Chinese national standard falcon (CNS) A4 specification (210X 297 mm) is applicable through the paper wave scale 12 (please read the precautions on the back before filling out this page) -installed ' A7 B7 printed by the Bureau of Consumer Products Co., Ltd. V. Description of the invention () 13 The reverse effect of the size stability of the cell wall to the outside. The polyol component reacts with the organic polyisocyanate component to produce a rigid polyurethane foam It is preferably carried out in the presence of a catalyst or a foam stabilizer. The catalyst used is not limited, and any well-known catalyst can be used. Preferably, the catalyst is an amine catalyst, including, for example, tetramethylhexamethylenediamine (TMHDA, supplied as KAORIZER N0.1 (Kao KK) or TOYOCAT-MR (Toso Κ · K.)), Pentamethyl diethylidene tris Amine (PMDETA, supplied as KA 0 RI ZERH 0.3 (K a ο K. K.) Or T 0 Y 0 CAT-DT (T 〇s ο K · K.)), One of the triethylene diamines Dipropylene glycol solution (usually abbreviated as TEDAL-33, supplied as DABC0-33LV (Air Products)), or bis (2-methylaminoethyl) ether (supplied as TOYOCAT ET (Toso K.K.)). The catalyst can be used alone or in a mixture. Amine catalysts other than those exemplified above or organic gold S compounds can also be used as catalysts if necessary. Especially when spray-foaming to produce rigid foams, such as organometallic compounds of lead octoate and dibutyltin dilaurate. The catalyst is usually used in an amount of 0.01 to 5 wt% based on the polyol used. The foam stabilizer used is not limited, and any foam stabilizer can be used. The foam stabilizer used includes, for example, B-8404, B-8407 or B-8 4 2 5 (supplied by G 〇1 d S ch in idt), F-3 0 5, F-3 4 5 or F-3 7 3 (by

Shin-Etsu Kagaku Kogyo K. K.供應),SH-19:M 由 Toray-Shin-Etsu Kagaku Kogyo K. K.), SH-19: M by Toray-

Dow Corning供應),或 L-5420, L-5430或 L-5350(由 H ί p p ο n U n i c a r供應)。除了以上所舉之製造硬質聚胺基甲 酸酯發泡體之泡沫安定劑以外,亦可使用例如β-80Ι7(由 本紙張尺度適用中國國家梂準(CNS ) Α4規A· ( 210Χ297公釐) 】? (請先讀背面之注意事項再填寫本頁) -裝 訂 線 311920 B7Dow Corning), or L-5420, L-5430 or L-5350 (supplied by H ί p p ο n U n i c ar). In addition to the above-mentioned foam stabilizers for manufacturing rigid polyurethane foams, for example, β-80Ι7 can be used (from the paper standard applicable to China National Standards (CNS) Α4 regulation A · (210Χ297mm) 】? (Please read the precautions on the back before filling in this page) -Binding line 311920 B7

修正I 年月O C? I A 7 換,#補七i A7 五、發明説明(14)Amend I year month O C? I A 7 to change, # 补 七 i A7 V. Invention description (14)

Gold Schmidt供應)之製造軟質聚胺基甲酸酯發泡體之較 活性泡沫安定劑。 以使用多元醇成份為基準,可使用0.5-5重童X之量的 泡沫安定劑。 必要時,可使用例如難燃劑,抗氣化劑或箸色劑等任 合添加劑。例如宜使用磷酸#(氣丙)酯(TCPP)作為難燃劑 當製備多元醇之預混物時,必要時亦可使用例如碩酸 伸丙酯之黏度降低劑。 硬質聚胺基甲酸酯發泡體可藉任何傳統方法製得。將 如上所示之原料予以均勻混合且使混合物在高壓發泡機中 反應。本發明之硬質聚胺基甲酸酯發泡體宜具有約20-50kg/ciH3之密度。 本發明現將參照實施例和參考例予以更詳細之説明, 然而,本發明並不偈限於這些實例。 實施例和參考例中所用之材料為如下: 多元醇A : 藉首先添加3莫耳份之環氣乙烷至1莫耳份之N -胺基乙 基六氫吡畊,然後添加3.8莫耳份之環氧丙烷至1莫耳份之 Η-胺基乙基六氫吡阱製得之加成物,具有3 5 3 m gKOH/g之翔 值,2900mPa.sec (厘泊)之25C下之黏度和在分子末端14¾ 之一级羥基含量,在本發明之範圍内。 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) (請先閱讀背面之注意事項再填寫本頁)Gold Schmidt) supplied flexible foam stabilizers for the manufacture of flexible polyurethane foams. Based on the use of polyol ingredients, a foam stabilizer in an amount of 0.5-5 heavy child X can be used. If necessary, any additives such as flame retardants, anti-gasification agents or colorants can be used. For example, it is advisable to use # (gas propyl) phosphate (TCPP) as a flame retardant. When preparing a premix of polyols, a viscosity-reducing agent such as propylene glycolate may also be used if necessary. The rigid polyurethane foam can be prepared by any traditional method. The raw materials shown above were uniformly mixed and the mixture was reacted in a high-pressure foamer. The rigid polyurethane foam of the present invention preferably has a density of about 20-50 kg / ciH3. The present invention will now be described in more detail with reference to examples and reference examples, however, the present invention is not limited to these examples. The materials used in the examples and reference examples are as follows: Polyol A: By first adding 3 mol parts of ring gas ethane to 1 mol parts of N-aminoethylhexahydropyridine, then adding 3.8 mols Parts of propylene oxide to 1 mole parts of H-aminoethyl hexahydropyridine trap adduct, with a flying value of 3 5 3 m gKOH / g, 2900mPa.sec (centipoise) at 25C The viscosity and the content of the first-order hydroxyl group at the end of the molecule are within the scope of the present invention. The size of this paper is applicable to the Chinese National Standard (CNS) A4 (210X297mm) (Please read the precautions on the back before filling this page)

L 經濟部中央橾準局員工消費合作社印製 Γ _______ / 、________ Ϊ ^ i—f nn tm i ---^^ vm iffn I i^J i 1^1^1 · 14 (修正頁) 311920 修正 年月曰、 两多*^9補充 A7 B7 五、發明説明(15 ) 經濟部中央標準局員工消費合作社印製 劣元醇B : 藉 首 先 添 加 2 . 5莫耳份之環 氣乙烷至 1莫耳之 N - 胺 基 乙 基 氫 吡 畊 9 且 然 後添加 3 . 0莫 耳份之環 氣丙烷至1 莫 耳 份 之 N- 胺 基 乙 基 氫 吡畊所 製得之加成物, 具有4 0 5 m gKOH/ g之羥值, 3 5 0 0 m Pa .s e c (厘泊)之2 5 1C下黏度,和 19¾之分 子 終 端 之 一 级 羥 基 含量和 分子終端之二級羥基, 在 本 發 明 之 範 圍 内 〇 多 元 醇 C : 藉 添 加 5 . 8莫耳份之環氣丙 烷至1莫耳份之 胺 基 乙 基 _L. 氫 吡 肼 製 得 之 加 成物, 具有36〇BgKOH/g之羥值 9 55 00 m P a . s e C ( 厘 泊 )之25它下黏 度和在分 子終端之二级羥 基 9 在 本 發 明 範 圍 之外。 多 7Π 醇 D ·· 藉 首 先 添 加 3 . 5莫耳份之環 氣丙烷至 1莫耳份 之 N - 胺 基 乙 基 氫 吡 姘 t 且 然後添 加2 . 0 莫耳份之 環氧乙烷至1 莫 耳 份 之 H- 胺 乙 基 —1^. 氫 吡肼, 具41 5 mgKOH/s之經值,3500m Pa • s e C ( 厘 泊 )之251C下黏度, 25¾在分子終端之二级 羥 基 含 量 > 本 發 明 範 圍 之 外 0 多 7Π 醇 R : 藉 首 先 添 加 4 . 0荚耳份之環 氣乙烷至 1莫耳份 之 N - 胺 基 乙 基 -J * 氫 吡 畊 所 製 得之加 成物, 具有551 m g K 0 H / g 之 羥 值 9 5800mPa,sec(厘泊)之25C下黏度,和100¾在分子終端之 一级羥基,本發明範圍之外。 本紙張尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 15 (修正頁) --------^裝------訂-----卜A (請先閲讀背面之注意事項再填寫本頁) 經濟部中央梂隼局—工消资合作社印製 A7 B7五、發明説明() 16 劣元醇F : 藉添加環氣丙烷至Μ糖和甘油之混合物製得之加成物 ,具有450aigK0H/g之徑值和6000mPa.sec (厘泊)之25t下 黏度。 多完醇G : _ 藉添加環氣丙烷至甲代苯二胺和三(羥乙基)胺之混合 物所製得之加成物,具有460mgK0H/s之羥值和5500nPa. s e c (厘治)之2 5 t:下黏度。 劣朵醇Η : 藉添加4.0莫耳份之環氣丙烷至1莫耳份之乙二胺所製 得之加成物,具有770mgK0H/g之翔值和50000mPa.sec (厘 泊)之2 5 υ下黏度。 劣元醇Τ : 藉添加環氣丙烷至甲代苯二胺和三(羥乙基)胺之Μ合 物所製得之加成物,具有455mgK0H/g之羥值和lOOOOraPa. s e c (厘泊)之2 5 t:下黏度。 縮窵: CT:乳化時間;開始混合材料之後,反應混合物變成乳 狀所需之時間(秒) G T :凝膠時間;開始混合材料之後,反應混合物變成黏 稠狀且具有凝膠強度所需之時間(秒) TMHDA:四甲基己二胺(胺催化劑) TCPP :磷酸蓥(氯丙)酯 UpUnate M-20S:多沖甲基多苯基多異氰酸酯,具有 (請先閱讀背面之注意事項再填寫本頁) -il^i fn i ·}' I In n· m) ml .L Printed by the Employees ’Consumer Cooperative of the Central Department of Economics of the Ministry of Economy Γ _______ /, ________ Ϊ ^ i—f nn tm i --- ^^ vm iffn I i ^ J i 1 ^ 1 ^ 1 Year and month, two more * ^ 9 supplement A7 B7 V. Description of invention (15) Printed inferior alcohol B by the employee consumer cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs: First add 2.5 mol of ring gas ethane to 1 Mol of N-aminoethyl hydropyrene 9 and then add 3.0 mol of cyclopropane to 1 mol of N-aminoethyl hydropyrene, an adduct prepared by The hydroxyl value of 4 0 5 m gKOH / g, the viscosity at 2 5 1C of 3 5 0 0 m Pa .sec (centipoise), and the content of the primary hydroxyl group at the molecular terminal of 19¾ and the secondary hydroxyl group at the molecular terminal. Within the scope of the invention 〇 Polyol C: by adding 5.8 moles of cyclopropane to 1 moles of amino ethyl_L. Hydrogen pyrazide made of adduct, with 36〇BgKOH / The hydroxyl value of g is 9 55 00 m P a. se C (centipoise) 25 and its viscosity and its molecular terminal Hydroxy-level outside the scope of the present invention 9. More than 7Π alcohol D. By first adding 3.5 mol parts of cyclopropane to 1 mol parts of N-aminoethylhydropyridine t and then adding 2.0 mol parts of ethylene oxide to 1 Molar part of H-aminoethyl—1 ^. Hydropyrazine, with a value of 41 5 mgKOH / s, 3500m Pa • se C (centipoise) viscosity at 251C, 25¾ secondary hydroxyl group at the molecular terminal Content > outside the scope of the present invention 0 more than 7Π alcohol R: by first adding 4.0 pods of ring gas ethane to 1 moles of N-aminoethyl-J * hydropyridine The adduct has a hydroxyl value of 551 mg K 0 H / g of 9 5800 mPa, a viscosity of 25 C at sec (centipoise), and a first-order hydroxyl group at the molecular terminal of 100¾, which is outside the scope of the present invention. The size of this paper is applicable to the Chinese National Standard (CNS) A4 specification (210X297mm) 15 (revision page) -------- ^ installed ------ order ----- Bu A (please read first (Notes on the back and then fill out this page) A7 B7 Printed by the Ministry of Economic Affairs Central Bureau of Industry and Commerce-Cooperatives Co., Ltd. V. Description of invention () 16 Poor alcohol F: prepared by adding a mixture of cyclopropane to M sugar and glycerin The adduct has a diameter value of 450aigK0H / g and a viscosity of 25t at 6000mPa.sec (centipoise). Polyalcohol G: _ An adduct prepared by adding cyclopropane to a mixture of tolylenediamine and tris (hydroxyethyl) amine, has a hydroxyl value of 460mgK0H / s and 5500nPa.sec (Chr) 2 5 t: Lower viscosity. Inferior alcohol H: an adduct prepared by adding 4.0 mole parts of cyclopropane to 1 mole parts of ethylenediamine, having a fly value of 770 mgK0H / g and 250,000 of 50000 mPa.sec (centipoise) υ Lower viscosity. Inferior alcohol Τ: an adduct prepared by adding cyclopropane to the M compound of tolylenediamine and tris (hydroxyethyl) amine, having a hydroxyl value of 455mgK0H / g and 1000 rasPa. Sec (centipoise ) Of 2 5 t: lower viscosity. Shrinkage: CT: emulsification time; the time required for the reaction mixture to become milky after starting to mix materials (seconds) GT: gel time; the time required for the reaction mixture to become viscous and having gel strength after starting to mix materials (Seconds) TMHDA: Tetramethylhexamethylenediamine (amine catalyst) TCPP: Thulium Phosphate (chloropropyl) ester UpUnate M-20S: Polymethyl polyphenyl polyisocyanate with (please read the precautions on the back before filling in (This page) -il ^ i fn i} 'I In n m) ml.

-IT -夂丨線-IT-夂 丨 Line

mu nn irj 4ml ^nn i 11- 1 - —/d m^— m^— - - I —--I —·1, ^im I 本紙浪又度逍用中國國家橾準(CNS ) A4规格(210X297公釐) 經濟部中央橾隼局具工消費合作社印裂 A7 B7 五、發明説明() 17 180mPa.sec (厘治)之 25¾ 下黏度,由 Takeda Badische Urethane Kogyo K. K,供應 Millionate MR-100:多伸甲基多苯基多異氣酸酯,具 有170iaPa.sec(厘泊)之25T;下黏度,由Nippon Polyurethane K. K.供應。 發泡體件皙_暑 以製得之發泡體的中央部份進行測量。 壓縮強度: 在10¾壓縮下,沿箸發泡體升起之方向測量壓縮強度 0 尺寸安定性: 在- 30t:下靜置24小時後或在50t , 95¾相對濕度下靜 置2 4小時,於平行或垂直於發泡方向之方向測量發泡體之 尺寸安定性。 多元醇/\餺诰> 宮例 將15kg之量的N -胺基乙基六氫吡畊置於^提供加熱裝置 和攪拌裝置之可加壓之70升容量反應器。在以氮氣取代反 應器内之大氣之後,加熱反應器之内容物至110°C,且然 後在4小時之期間連缅添加1 5 . 3 k g之環氣乙烷。添加之後, 使反應混合物老化1小時以便完成環氣乙烷和N -胺基乙基 六氫吡阱之反應。 添加125^之量的燒瓶中之氫氣化鉀於反應混合物中。 於保持反應混合物在1 1 0 - 1 2 0 t:之溫度時.,在4小時期間連 續添加2 5 . 6 kg之環氣丙烷。於添加之後,加熱反應混合物 本紙张尺度遑用中國國家標率(CNS ) A4規格(210 X 297公釐) 飞7 ^ 訂 ^ *务 (請先閱讀背面之注意事項再填寫本頁) 311820 at B7 經濟部令央揉準局貝工消費合作杜印製 五、發明说明() 18 至120-130¾之溫度且在此溫度下老化1小時以完成環氧丙 院之反應。 溶解1 3 0 S之量的二結晶水草酸於1升水中以製備一溶 液。添加此溶液至反應混合物以便去活化或中和氫氧化鉀 ,且然後將此反應混合物予以去水。 藉使用壓濾機由反應混合物壓榨反應混合物而由反應 混合物中移除氫氧化鉀與草酸反應所製得之最終固態草酸 鉀,而獲得多元醇A。 元袤分析: C Η Ν 實測值 60.43 10.53 8.87 理論值 60.87 10.35 8.73 理論值烧:假設氣伸乙基之平均數,ηι+η2 + π3 = 3.0和氧 伸丙基之平均數,mi+m2 + m3 = 3.8所.計.算得到。 红外線趿牧(T R )来譜f波數.e m — Π : 第1圖表示多元醇A之紅外線吸收光譜; 11 0 0附近:-C - 0 - C - 伸張 1500附近:-C-H _折擺動 2800-3000附近:-C-Η 伸張 晋子核磁共振光(乃· PP1B): 第2圖表示多元醇A之NMR光譜; 1.1附近:甲基之三値質子 2.5附近:-NCH2CH2N-基之四個質子 2.7附近:鍵結至4(^2(:[{2〇-基之氮上之伸甲基的兩 本紙伕尺度適用中國國家梯準(CNS ) A4规格(210X297公釐) 18 (請先閲讀背面之注意事項再填寫本頁) •裝 訂 '線 經濟部中央橾隼局只工消资合作杜印裝 A7 B7 五、發明説明() 19 値質子。 3.1-3.8附近:-(:112〇~基之兩個質子 3.9附近‘·氣伸丙基之次甲基質子mu nn irj 4ml ^ nn i 11- 1-— / dm ^ — m ^ —--I —-- I — · 1, ^ im I This paper is used again and again with Chinese National Standard (CNS) A4 specification (210X297 Mm) The Central Falcon Bureau of the Ministry of Economic Affairs printed A7 B7. 5. Description of the invention () 17 180mPa.sec (Lizhi) with a viscosity of 25¾, supplied by Takeda Badische Urethane Kogyo K. K, Millionate MR-100 : Polymethylene polyphenyl polyisogasate, with 25T of 170iaPa.sec (centipoise); lower viscosity, supplied by Nippon Polyurethane KK. The foam body is made by measuring the central part of the foam. Compressive strength: Under 10¾ compression, measure the compressive strength along the direction in which the foam rises. Dimensional stability: After standing at -30t: 24 hours or standing at 50t, 95¾ relative humidity for 24 hours, at Measure the dimensional stability of the foam in a direction parallel or perpendicular to the foaming direction. Polyol / \ 馎 诰 > Gong example An amount of 15 kg of N-aminoethylhexahydropyrrolidine was placed in a pressurizable 70-liter capacity reactor provided with a heating device and a stirring device. After replacing the atmosphere in the reactor with nitrogen, the contents of the reactor were heated to 110 ° C, and then 15.3 kg of ring gas ethane was added continuously over a period of 4 hours. After the addition, the reaction mixture was aged for 1 hour to complete the reaction of ring gas ethane and N-aminoethylhexahydropyridine trap. An amount of 125 ^ potassium hydroxide in the flask was added to the reaction mixture. While maintaining the temperature of the reaction mixture at 1 1 0-1 2 0 t :, 25.6 kg of cyclopropane was continuously added during 4 hours. After addition, the reaction mixture is heated. The paper scale is based on the Chinese National Standard (CNS) A4 specification (210 X 297 mm). Flying 7 ^ Order ^ * Business (please read the precautions on the back and fill in this page) 311820 at B7 The Ministry of Economic Affairs ordered the Central Bureau of Industry and Fisheries to cooperate in the printing of Du. V. Invention description () 18 to 120-130¾ and aging at this temperature for 1 hour to complete the reaction of the propylene oxide institute. A solution of dicrystalline water oxalic acid in an amount of 1 3 0 S was dissolved in 1 liter of water to prepare a solution. This solution was added to the reaction mixture in order to deactivate or neutralize potassium hydroxide, and then the reaction mixture was dehydrated. Polyol A is obtained by squeezing the reaction mixture from the reaction mixture using a filter press to remove the final solid potassium oxalate prepared by the reaction of potassium hydroxide and oxalic acid from the reaction mixture. Yuan Yuan analysis: C Η Ν Measured value 60.43 10.53 8.87 Theoretical value 60.87 10.35 8.73 Theoretical value Burning: Assuming the average number of gas-extended ethyl groups, ηι + η2 + π3 = 3.0 and the average number of oxypropylene groups, mi + m2 + m3 = 3.8 calculated. Infrared Zhumu (TR) spectrum f wave number.em — Π: The first figure shows the infrared absorption spectrum of polyol A; around 11 0 0: -C-0-C-around extension 1500: -CH _fold swing 2800 Near -3000: -C-Η extended Jinzi nuclear magnetic resonance light (NO · PP1B): Figure 2 shows the NMR spectrum of Polyol A; near 1.1: Methyl trivalent protons near 2.5: -NCH2CH2N-based four Near Proton 2.7: The two paper bond scales bonded to 4 (^ 2 (: [{2〇-based nitrogen on methyl are applicable to China National Standards (CNS) A4 specification (210X297mm) 18 (please first Read the precautions on the back and then fill out this page) • Staples' Line Ministry of Economic Affairs Central Falcon Bureau only works with consumers to cooperate with Du Printed A7 B7 V. Description of invention () 19 Protons near 3.1-3.8:-(: 112〇 ~ Two protons of the base are near 3.9 'methine protons

使用三氣乙酐將多元醇A三氟乙醯化而獲得酯化合物 。第3圖表示酯化合物之NMR光譜。 g旃例T . 較例T筘T T 如表1所示之配方,以手涯合材料且以自由膨脹發泡 法製得發泡體(自由發泡發泡體)。 添加泡沫安定劑,催化劑,難燃劑和發泡劑至200重 量份之多元醇成份,且調節溫度至20±1TC,以製備多元醇 預混物。 將有機多異氛酸酯(Luplanate M-20S)調節至20±11C 之溫度且然後添加至多元醇預混物。混合物攪拌3至5秒之 後立即倒入其内置有分離紙之25cm立方木箱,以獲得硬質 發泡體。 依表2和3所示之配方,以如上相同之方式製得硬質發 泡體。 材料之反應性和所得發泡體之性質皆示於表1至3。 第4函表示實施例I和比較例I I和I I I中,H C F C - 1 4 1 b用 «與所得發泡體之密度的關偽。當使用固定之相對於多元 醇成份之H C F C - 1 4 1 b量,實施例I獲得較比較例I和I I為小 之密度。 若不管所用之多元醇成份發泡效率不變,應導致具有 相同發泡體密度之硬質發泡髏。然而.如第4圖所示,可 本紙張尺度適用中國國家標準(CNS)八4规格(210X297公簸) ,„ (請先閲讀背面之注意事項再填寫本頁) J, -装. 訂 S11S20 A7 B7 五、發明説明() 20發現所製得發泡體間之發孢體密度有明潁不同,且比不同 M份 環部 序作 依t 之物 明成 發加 本之 用畊 使吡 可氫 , 六 此基 因乙 Ο 基 同胺 不H-之與 率烷 效丙 泡氧 發環 於 和 因烷 導 乙 具 體 泡 。 發 體之 泡得 發製 質所 硬中 之2) 度表 密ί 低 較例 有較 具比 得 , 獲知 可可 份步 成 一 醇進 元如 多 之 5 2 性 定 有安 寸 尺 之 良 不 有 具 而 縮 收 之 胞 徹 因 但 度 密 之 3 0 / S .k 例 施 實 地 對 相 具 體 泡 發 之 得 裂 所 中 \1/ 1X 表 尺 之 越 優 有 却 但 小 為 體 泡 發 述 上 較 度 密 之 3 瓜 / 5 k 6 4 2 性 定 安 寸 (請先閣讀背面之注意事項再填寫本育) m nn ml ml ·Trifluoroacetic anhydride is used to trifluoroacetate Polyol A to obtain an ester compound. Figure 3 shows the NMR spectrum of the ester compound. g Example T. Comparative Example T Reed T T As shown in Table 1, the foam (free-foamed foam) was prepared by using the materials of the hand and using the free expansion foaming method. Add foam stabilizer, catalyst, flame retardant and foaming agent to 200 parts by weight of polyol component, and adjust the temperature to 20 ± 1TC to prepare polyol premix. The organic polyisocyanate (Luplanate M-20S) was adjusted to a temperature of 20 ± 11C and then added to the polyol premix. After the mixture was stirred for 3 to 5 seconds, it was immediately poured into a 25 cm cubic wooden box in which the separation paper was built to obtain a rigid foam. According to the formulations shown in Tables 2 and 3, rigid foams were prepared in the same manner as above. The reactivity of the material and the properties of the resulting foam are shown in Tables 1 to 3. The fourth letter shows that in Example I and Comparative Examples I I and I I I, H C F C-1 4 1 b uses «to check the density of the obtained foam. When a fixed amount of H C F C-1 4 1 b relative to the polyol component is used, Example I obtains a lower density than Comparative Examples I and I I. If the foaming efficiency remains unchanged regardless of the polyol component used, it should result in a rigid foam with the same foam density. However, as shown in Figure 4, the paper size is applicable to the Chinese National Standard (CNS) 84 specifications (210X297 bumps), (please read the precautions on the back before filling this page) J, -install. Order S11S20 A7 B7 V. Description of the invention () 20 It was found that the density of the sporozoites between the foams produced was different from that of the rhizome, and that the order of the M parts of the ring part was different according to t. , Sixth this gene ethyl amine is not H- and the rate is equivalent to the effect of propylene oxygen hair ring and due to the alkyl lead to the specific bubble. The hair body is obtained by the hair quality. 2) The degree of density is low The comparative example has a better comparison. It is known that cocoa can be transformed into a single alcohol with a large amount of 5 2. In fact, the best place for the specific bubble hair \\ 1 1X scale is better, but it is small, and the body bubble is more dense. 3 melons / 5 k 6 4 2 sexual stability (please read the first (Notes on the back and fill in this education) m nn ml ml ·

JJ

Ji ts. I- — -1-- --- 1Ji ts. I- — -1-- --- 1

,1T 17線 經濟部中央梂準局具工消費合作杜印製 i^n 1 11 nn · 本紙張尺度遑用中國國家標準(CNS ) A4见格(2l〇X297公釐) ο 2 A7 7 Β 五、、發明説明(21) 表1 經濟部中央揉準局負工消費合作杜印製 實施例I 1 2 3 4 5 原料(重量比) 多元醇A 20 20 20 20 20 多元醇F 40 40 40 40 40 多元醇G 40 40 40 40 40 TCPP 10 10 10 10 10 SH-193 1.5 1.5 1.5 1.5 1.5 水 2.5 2.5 2.5 2.5 2.5 TMHDA 0.45 0.45 0.45 0.45 0.45 HCFC-141b 17 20 23 26 29 Luplanate M-20S 156 156 156 156 156 異氣酸酯指數 110 110 110 110 110 反應性 CT (sec.) 11 11 11 11 11 GT (sec·) 51 51 54 58 58 發泡體性質 自由發泡體密度(kg/m3) 27.4 26.1 24.6 23.6 22.6 尺寸安定性 (-30C下靜置 24小時之後) 平行於發泡方向U) 0.11 0 0 0.14 大 垂直於發泡方向U) -0.13 -0.13 0 -3.0 大 ®縮強度(kg/cm2) (10%壓縮之下) 平行於發泡方向U) 1.68 1.62 1.31 1.31 0.17 垂直於發泡方向U) 0.43 0.41 0.38 0.31 0.25 本紙張尺度速用中國國家標準(CNS ) A4规格(210X297公釐) (請先閲讀背面之注意事項再填寫本頁), 1T 17-line Ministry of Economic Affairs Central Bureau of Economic Cooperation and Industry Cooperative Printing and Printing Du ^ i 1 11 nn · This paper size is based on China National Standard (CNS) A4 see grid (2l0X297mm) ο 2 A7 7 Β V. Description of the invention (21) Table 1 Example of du printing by the Ministry of Economy Central Bureau of Accreditation and Consumer Cooperation I 1 2 3 4 5 Raw materials (weight ratio) Polyol A 20 20 20 20 20 Polyol F 40 40 40 40 40 Polyol G 40 40 40 40 40 TCPP 10 10 10 10 10 SH-193 1.5 1.5 1.5 1.5 1.5 Water 2.5 2.5 2.5 2.5 2.5 TMHDA 0.45 0.45 0.45 0.45 0.45 HCFC-141b 17 20 23 26 29 Luplanate M-20S 156 156 156 156 156 Isoarate index 110 110 110 110 110 Reactive CT (sec.) 11 11 11 11 11 GT (sec ·) 51 51 54 58 58 Foam properties Free foam density (kg / m3) 27.4 26.1 24.6 23.6 22.6 Dimensional stability (after standing at -30C for 24 hours) Parallel to the foaming direction U) 0.11 0 0 0.14 Large perpendicular to the foaming direction U) -0.13 -0.13 0 -3.0 Large® shrinkage strength (kg / cm2) (under 10% compression) parallel to the foaming direction U) 1.68 1.62 1.31 1.31 0.17 perpendicular to the foaming direction U) 0.43 0.41 0.3 8 0.31 0.25 This paper uses the Chinese National Standard (CNS) A4 specifications (210X297mm) (please read the precautions on the back before filling this page)

It --aIt --a

7 7 A B 五、發明説明() 22 表2 比較例I 1 2 3 4 5 原料(重量比) 多元醇F ~ 50 50 50 50 50 多元醇G 50 50 50 50 50 TCPP 10 10 10 10 10 SH-193 1.5 1.5 1.5 1.5 1.5 水 2.5 2.5 2.5 2.5 2.5 TMHDA 2.0 2.0 2.0 2.0 2.0 HCFC-141b 20 23 26 29 32 Lupianate M-20S 162 162 162 162 162 異氰醆酯指數 110 110 110 no 110 反應性 CT (sec ·) 13 13 13 13 13 GT (sec ·) 50 54 54 56 57 發泡體性質 經濟部令央橾準局—工消費合作社印製 自由發泡體密度(ks/m3) 尺寸安定性 (-301下靜置 24小時之後) 29.1 27.8 26.4 25.1 24.0 平行於發泡方向U) 0 0.18 0.13 大 大 垂直於發泡方向(¾) 壓縮強度(ks/cat2) (10¾壓縮之下) 0 -0.13 -0.90 大 大 平行於發泡方向U) 2.22 2.03 1.78 1.55 1.33 垂直於發泡方向U) 0.59 0.49 0.39 0.32 0.21) 本紙張尺度適用中國國家揉準(CNS ) A4规格(210X297公釐) 22 (請先閲讀背面之注意事項再填寫本j)7 7 AB V. Description of invention () 22 Table 2 Comparative Example I 1 2 3 4 5 Raw materials (weight ratio) Polyol F ~ 50 50 50 50 50 Polyol G 50 50 50 50 50 TCPP 10 10 10 10 10 SH- 193 1.5 1.5 1.5 1.5 1.5 Water 2.5 2.5 2.5 2.5 2.5 TMHDA 2.0 2.0 2.0 2.0 2.0 HCFC-141b 20 23 26 29 32 Lupianate M-20S 162 162 162 162 162 Isocyanate index 110 110 110 no 110 Reactive CT (sec ·) 13 13 13 13 13 GT (sec ·) 50 54 54 56 57 Properties of foams The Ministry of Economy ordered the Central Bureau of Industry and Commerce-Cooperatives to print free foam density (ks / m3) Dimensional stability (-301 After standing for 24 hours) 29.1 27.8 26.4 25.1 24.0 parallel to the foaming direction U) 0 0.18 0.13 greatly perpendicular to the foaming direction (¾) compressive strength (ks / cat2) (under 10¾ compression) 0 -0.13 -0.90 greatly (Parallel to the foaming direction U) 2.22 2.03 1.78 1.55 1.33 Perpendicular to the foaming direction U) 0.59 0.49 0.39 0.32 0.21) This paper size is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm) 22 (Please read the back side first Note and then fill in this j)

A7 B7 五、發明説明(23 ) 表3 經濟部中央揉準局貝工消費合作杜印製 比較例II 1 2 3 4 5 原料(重量比) 多元醇C 20 20 20 20 20 多元醇F 40 40 40 40 40 多元醇G 40 40 40 40 40 TCPP 10 10 10 10 10 SH-193 1.5 1.5 1.5 1.5 1.5 水 2.5 2.5 2.5 2.5 2.5 TMHDA 0.6 0.6 0.6 0.6 0.6 HCFC-141b 17 20 23 26 29 Luplanate M-20S 156 156 156 156 156 異氰酸酯指數 110 110 110 110 110 反應性 CT (sec.) 12 12 12 12 12 GT (sec·) 47 49 50 52 53 發泡體性質 自由發泡謾密度(kg/m3) 28.4 27.1 25.8 ' 24.6 23.5 尺寸安定性 (-30Ό下靜置 24小時之後) 平行於發泡方向U) 0 0.15 0.12 0.12 大 垂直於發泡方向α) 0 -0.14 0 -0.62 大 壓縮強度(kg/cm2) (10%壓縮之下) 平行於發泡方向U) 1.75 1.87 1.55 1.45 1.33 垂直於發泡方向α) 0.56 0.44 0.42 0.33 0.30 本紙張尺度適用中國S家標率(CNS ) A4规格(210X297公釐) --------(-裝------訂-----^ 0 (請先閱讀背面之注意事項再填寫本頁) 23 311S20 附 件 經濟部中央標準局員工消費合作社印製 A7 B7 η Μ-A7 B7 V. Description of the invention (23) Table 3 Comparative example of Beigong consumer cooperation du printing by the Central Ministry of Economic Affairs of the Ministry of Economic Affairs II 1 2 3 4 5 Raw materials (by weight) Polyol C 20 20 20 20 20 Polyol F 40 40 40 40 40 Polyol G 40 40 40 40 40 TCPP 10 10 10 10 10 SH-193 1.5 1.5 1.5 1.5 1.5 Water 2.5 2.5 2.5 2.5 2.5 TMHDA 0.6 0.6 0.6 0.6 0.6 HCFC-141b 17 20 23 26 29 Luplanate M-20S 156 156 156 156 156 Isocyanate index 110 110 110 110 110 Reactivity CT (sec.) 12 12 12 12 12 GT (sec ·) 47 49 50 52 53 Foam properties Free foam density (kg / m3) 28.4 27.1 25.8 '24.6 23.5 Dimensional stability (after standing at -30Ό after 24 hours) parallel to the foaming direction U) 0 0.15 0.12 0.12 substantially perpendicular to the foaming direction α) 0 -0.14 0 -0.62 large compressive strength (kg / cm2) ( 10% compression) parallel to the foaming direction U) 1.75 1.87 1.55 1.45 1.33 perpendicular to the foaming direction α) 0.56 0.44 0.42 0.33 0.30 The paper size is applicable to China S home standard rate (CNS) A4 specification (210X297 mm)- ------- (-install ------ order ----- ^ 0 (Please read the notes on the back before filling This page) 23 311S20 Attachment Printed by the Employees Consumer Cooperative of the Central Bureau of Standards of the Ministry of Economic Affairs A7 B7 η Μ-

五、發明説明(2 4 )實施例I I,比較例I I I和I V 表 依 -ΠΤΤ 藉 式 方 之 同 相 I 例 施 實 如 以 方 配 之 示 所 體 泡 發 得 製 法 泡 發 由 環 加 添 幹 骨 醇 元 多 視 度 程 之 低 降 度 密 示 所 中 5 表 如 進 ο 置 位 之 烷 乙 氧 農 泡 發 之 得 製 中 α有 If具 II下 例件 較條 比溫 在 高 於及 較濕 相在 是 體 的泡 到發 解明 了發 步本 烷 乙 氣 環 加 添 僅 由 用 使 0 係 體 泡 發 其 〇 尤 性 , 定中 安IV 寸例 尺較 之 比 良 改 發溫 被 高 性和 應 濕 反在 之體 料泡 材發 〇 得 得所 製現 所發 份亦 成 且 醇 , 元應 多反 之制 得控 製法 所無 劑而 始大 起太 至 現 性 定 安 寸 尺 之 差 常 非 有 具 下 件 條 本紙張尺度適用中國國家標準(CMS ) A4規格(210X 297公釐) 2 4 (修正頁) (請先閲讀背面之注意事項再填寫本頁) A7 B7 五、發明説明() 25 表4 實施例II 1 2 3 4 5 原料(重量比) 多元醇B 20 20 20 20 20 多元醇F 40 40 40 40 40 多元醇G 40 40 40 40 40 TCPP 10 10 10 10 10 SH-193 1.5 1.5 1.5 1.5 1.5 水 2.5 2.5 2.5 2.5 2.5 TMHDA 0.4 0.4 0.4 0.4 0.4 HCFC-141b 17 20 23 26 29 Lup 1 anate M-20S 159 159 159 159 159 異氰酸酯指數 110 110 110 110 110 反應性 CT (sec.) 9 9 9 9 9 GT (sec .) 50 50 51 52 52 發泡體性質 (請先閔讀背面之注意事項再填寫本頁) nn n^i— mfl flu^— { 秀 訂 <砝丨 經濟部中央樣準局男工消费合作社印製 自由發泡體密度(ks/ni3) 尺寸安定性 (-30t:下靜置 24小時之後) 27.6 26.3 24.8 23.8 22.7 平行於發泡方向U) 0.09 0 0 0.14 大 垂直於發泡方向U) 尺寸安定性 (50t: , 95¾濕度下 -0.08 -0.08 0 -0.9 大 靜置24小時以後) 0.75 0.80 0.83 0.92 1.01 垂直於發泡方向U) -0.95 -0.96 -1.11 -1.12 -1.19 本紙浪尺度適用中國國家橾準(CNS ) A4規格(210X 297公釐) 月 · 年1V. Description of the invention (2 4) Example II, comparative examples III and IV Table I-phases of the same phase by the -ΠΤΤ I Example of applying the foam as shown in the formula to prepare the foam by adding dry bone from the ring The low drop of the alcohol multi-view range is shown in the table 5 as shown in the following. The placement of the ethane ethoxynon bubble is made. In the case of α with If II, the following examples are more specific and higher than the specific temperature. It is clear from the body bubble to the hair that the hair is added to the ethane gas ring. The bubble is only made by the 0 system body. The IV size of the center is safer than that of Biliang. The temperature is high and the application should be high. Wet anti-existent foam materials can be obtained with good results and good alcohol content. Yuan Yingduo can make the control method without the agent, and the difference between the size and the size of the existing size is often not very small. The following paper size applies to the Chinese National Standard (CMS) A4 specification (210X 297mm) 2 4 (Amendment page) (Please read the precautions on the back before filling out this page) A7 B7 5. Description of invention () 25 Table 4 Example II 1 2 3 4 5 Raw materials (weight ratio) Polyol B 20 20 20 20 20 Polyol F 40 40 40 40 40 Polyol G 40 40 40 40 40 TCPP 10 10 10 10 10 SH-193 1.5 1.5 1.5 1.5 1.5 Water 2.5 2.5 2.5 2.5 2.5 TMHDA 0.4 0.4 0.4 0.4 0.4 HCFC-141b 17 20 23 26 29 Lup 1 anate M-20S 159 159 159 159 159 Isocyanate index 110 110 110 110 110 Reactive CT (sec.) 9 9 9 9 9 GT (sec.) 50 50 51 52 52 Foam properties (please read the precautions on the back and then fill in this page) nn n ^ i— mfl flu ^ — {Xiu Xiu < weight 丨 printed by the Male Workers' Consumer Cooperative of the Central Sample Bureau of the Ministry of Economic Affairs Free foam density (ks / ni3) size stability (-30t: after standing for 24 hours) 27.6 26.3 24.8 23.8 22.7 parallel to the foaming direction U) 0.09 0 0 0.14 large perpendicular to the foaming direction U) size Stability (50t :, 95¾ under humidity -0.08 -0.08 0 -0.9 after standing for 24 hours) 0.75 0.80 0.83 0.92 1.01 perpendicular to the foaming direction U) -0.95 -0.96 -1.11 -1.12 -1.19 This paper wave scale is suitable for China National Standard (CNS) A4 Specification (210X 297mm) Month · Year 1

7 7 A B JL'i ^11920 五、發明説明(26 ) 表5 比較例III 比較例IV 1 2 3 4 5 1 2 經濟部中央樣準局員工消費合作社印製 原料(重量比) 多元醇D 20 20 20 20 20 0 0 多元醇E 0 0 0 0 0 20 20 多元醇F 40 40 40 40 40 40 40 多元醇G 40 40 40 40 40 40 40 TCPP 10 10 10 10 10 10 10 SH-193 1.5 1.5 1.5 1.5 1.5 1.5 1.5 水 2.5 2.5 2.5 2.5 2.5 2.5 2.5 TMHDA 0.6 0.6 0.6 0.6 0.6 0.1 0.1 HCFC-141b 17 20 23 26 29 17 '20 Luplanate H-20S 159 159 159 159 159 167 167 異気酸酯指數 110 110 110 110 110 110 110 反應性 CT(sec.) 9 9 9 9 9 8 8 GT (sec·) 46 48 49 · 52 52 27 30 發泡體性質 自由發泡瞪密度(kg/n3) 尺寸安定性 29.0 27.6 26.1 24.8 23.5 25.1 23.5 (-30¾下靜置 24小時之後) 平行於發泡方向(50 0 0 0 0 大 0.14 大 垂直於發泡方向(¾) 尺寸安定性 0 0 -0.15 -0.17 大 -0.57 大 (5〇υ, 95¾濕度下 靜置24小時以後) 1 1.19 1.07 1.21 1.22 1.14 大 大 垂直於發泡方向(¾) -1.45 -1.43 -2.45 -2.09 -2.36 大 大 (請先閲讀背面之注意事項再填寫本頁) 本紙浪尺度適用中國國家標準(CNS ) A4規格(210X297公釐) 26 (修正頁) A7 B7五、發明説明(2 7 ) ILiL....M-Ι I L 依如下配方製備預混物。此預混物在2 5 C測得具有8 5 nPa.sec (厘泊)之黏度。 多元醇A 30重量份 多元醇Η 40 多元醇I 30 TCPP 15 SH-193 1.5 水 1.0 TEDA L-33 2.0 辛酸鉛(2050 0 . 3 HCFC- 1 41 b 50 (請先閲讀背面之注意事項再填寫本頁) --装 ---- 丁 經濟部中央梂率局貝工消f合作社印製 預混物和Μ丨llionate MR-100各以相同之體積份相互 混合且混合物以噴佈發泡機噴佈發泡於5mm厚之合板上。 發現所得發泡體具有如下之優越外觀和性質苴沒有層分離 或龜裂。 --▲-— 本紙浪尺度逍用中國國家橾準(CNS) A4規格(210X297公釐) 28 A7 B7 五、發明説明( 發泡體之層數 發泡體密度 尺寸安定性(-30Ό x24h「s) 與發泡方向平行 - 與發泡方向呈垂直 - 黏箸強度 熱導性 燃燒性(J IS A-9512) 3層 30.0kg/m3 0.37¾ 0.22¾ 2 . 56 kg/cm3 (發泡體破壊) 0.0160 Kcal/m.hr.t; 可自煩(4 0 s e c,3 7 m hi ) --------裝-- (請先閲讀背面之注意事項再填寫本頁) 訂------^ V, 經濟部中央揉率局負工消费合作社印製 本紙張尺度適用中國國家梯準(CNS ) A4規格(210X297公釐)7 7 AB JL'i ^ 11920 V. Description of invention (26) Table 5 Comparative example III Comparative example IV 1 2 3 4 5 1 2 Printed raw materials (weight ratio) of the employee consumer cooperative of the Central Bureau of Samples of the Ministry of Economy Polyol D 20 20 20 20 20 0 0 Polyol E 0 0 0 0 0 20 20 Polyol F 40 40 40 40 40 40 40 Polyol G 40 40 40 40 40 40 40 TCPP 10 10 10 10 10 10 10 SH-193 1.5 1.5 1.5 1.5 1.5 1.5 1.5 Water 2.5 2.5 2.5 2.5 2.5 2.5 2.5 TMHDA 0.6 0.6 0.6 0.6 0.6 0.1 0.1 HCFC-141b 17 20 23 26 29 17 '20 Luplanate H-20S 159 159 159 159 159 167 167 Isoester Index 110 110 110 110 110 110 110 Reactive CT (sec.) 9 9 9 9 9 8 8 GT (sec ·) 46 48 49 · 52 52 27 30 Foam properties Free foaming density (kg / n3) Size stability 29.0 27.6 26.1 24.8 23.5 25.1 23.5 (after standing at -30¾ for 24 hours) parallel to the foaming direction (50 0 0 0 0 large 0.14 large perpendicular to the foaming direction (¾) Dimensional stability 0 0 -0.15 -0.17 large -0.57 large (5〇υ, 95¾ after 24 hours under humidity) 1 1.19 1.07 1.21 1.22 1.14 greatly perpendicular to the foaming direction (¾) -1.45 -1.43 -2.45 -2.09 -2.36 Great (please read the precautions on the back before filling in this page) This paper wave scale is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm) 26 (revision page) A7 B7 Description of the invention (2 7) ILiL .... M-Ι IL is prepared according to the following formula. This premix has a viscosity of 8 5 nPa.sec (centipoise) measured at 25 C. Polyol A 30 Weight parts Polyol Η 40 Polyol I 30 TCPP 15 SH-193 1.5 Water 1.0 TEDA L-33 2.0 Lead octoate (2050 0. 3 HCFC- 1 41 b 50 (Please read the precautions on the back before filling this page)- -Installation ---- The premix and Mlllionate MR-100 printed by the Pinggongxiao F Cooperative of the Central Bureau of Economic Development of the Ministry of Economic Affairs are mixed with each other in the same volume and the mixture is sprayed and foamed with a spray foaming machine On 5mm thick plywood. It was found that the resulting foam had the following excellent appearance and properties. The sacks had no layer separation or cracking. -▲-This paper wave scale is easy to use Chinese National Standard (CNS) A4 specification (210X297mm) 28 A7 B7 5. Description of the invention (The number of layers of foam The density of foam density size stability (-30Ό x24h " s) parallel to the foaming direction-perpendicular to the foaming direction-viscous strength thermal conductivity flammability (J IS A-9512) 3 layers 30.0kg / m3 0.37¾ 0.22¾ 2 .56 kg / cm3 (foam壊 壊) 0.0160 Kcal / m.hr.t; can be annoying (4 0 sec, 3 7 m hi) -------- installed-(please read the precautions on the back before filling this page) Order- ----- ^ V, the paper printed by the Ministry of Economic Affairs of the Central Committee of the Ministry of Economic Affairs and Consumer Cooperatives of the paper standard is applicable to China National Standards (CNS) A4 specifications (210X297 mm)

Claims (1)

Ο 2 S 1 s 附件三Ο 2 S 1 s Annex III Η 經濟部中央標準局員工福利委員會印製 第83107042號專利申請案 申請專利範圍修正本 (85年10月29日) 1. 一種硬質聚胺基甲酸酯發泡體之製法,包括在發泡劑 存在下,使有機多異氛酸酯成份與多元成份反應, 其中多元醇成份包括具有下式之環氣烷與N-胺基乙基 六氫吡畊之加成物 /~\ /(EO) - (PO) -H H-(PO) - (EO) -N N-CH CH_N^ Π1 mi m3 n3 \__/ 2 2 '(EO) -(PO) -H n2 m2 其中EO為氣伸乙基,PO為氣伸丙基;ni, n2和n3為氣 伸乙基之平均數;111+112 + 113=:2.0-3.5: mi, m2 和 m3 為 氣伸丙基之平均數;且bi+bi2 + b3 = 3.0-6.0。 2. 如申請專利範圍第1項之製法,其中該加成物具有300 至430mgK0H/g之翔值。 3. 如申請專利範圍第1項之製法,.其中該多元醇成份含有 10-40重量ίϋ之量的加成物。 4. 如申請專利範圍第項之製法,其中該多元醇成份具有 300至 700agiC0H/g之經值。 5. 如申請專利範圍第1項之製法,其中發泡劑像至少一種 選自由氬化氣氟碩化合物,氫化氟碳化合物和全氟硕 化合物所組成之族群之另外氣氟磺化合物。 6. 如申請專利範圍第1項之製法,其中發泡劑係一種水和 至少一種另外氣氟碩化合物之混合物,該另外氣氟磺 本紙張尺度適用中國國家標準(CNS )A4規格(210 X 297公金) 1 H3 化合物傲選自由氫化氣氣碳化合物,氫化氟磺化合物 和全氣磺化合物所組成之族群。 ?.如申請專利範圍第1項之製法,其中發泡劑為1,1-二氣 -1 -氟乙院。 8. 如申請專利範圍第1項之製法,其中發泡劑為水和1,1-二氛-1-氟乙烷之混合物。 9. 如申請專利範圍第1項之製法,其中相對於100重量份 之多元醇成份使用15-40重量份之1,1-二氣-1-氟乙烷 和1.0-3.0重量份之水當作發泡劑。 10. 如申請專利範圍第1項之製法,其中該多異氡酸酯成份 為多伸甲基多苯基多異氰酸酯。 11. 一種硬質聚胺基甲酸酯發泡體,偽在發泡劑存在下, 使有機多異氛酸酯成份與多元醇成份反應所製得之硬 質聚胺基甲酸酯發泡體,其中多元醇成份包括具有下 式之環氧烷與N -胺基乙基六氫吡畊之加成物 N-CH-CH-N. 1 ' / 2 2 \(Ε〇) -(ρ〇) -η H-(P〇)m3-(EO)n^ (EO) -(PO) Ή 經濟部中央標準局員工福利委員會印製 基 乙 伸 氣 為 ο Ε 中 其 基 丙 伸 氣 為 3 π 和 2 η ; 數 數均 均平 平之 之基 基丙 乙伸 伸氣 氧為 為S3 且 η + + 1 和 本紙張尺度適用中國國家禮準(CNS )Α4規格(210 X 297公董)2Η Amendment of the patent scope of Patent Application No. 83107042 printed by the Employee Welfare Committee of the Central Standards Bureau of the Ministry of Economic Affairs (October 29, 85) 1. A method for manufacturing a rigid polyurethane foam, including foam In the presence of an agent, the organic polyisocyanate component is reacted with a multicomponent component, wherein the polyhydric alcohol component includes the adduct of cycloalkane and N-aminoethylhexahydropyridinium with the formula / ~ \ / (EO )-(PO) -H H- (PO)-(EO) -N N-CH CH_N ^ Π1 mi m3 n3 \ __ / 2 2 '(EO)-(PO) -H n2 m2 where EO is air stretch B Base, PO is air-extended propyl; ni, n2 and n3 are the average number of air-extended ethyl; 111 + 112 + 113 =: 2.0-3.5: mi, m2 and m3 are the average number of air-extended propyl; and bi + bi2 + b3 = 3.0-6.0. 2. The method as claimed in item 1 of the patent application scope, in which the adduct has a flying value of 300 to 430 mgK0H / g. 3. For example, the preparation method of the first item in the scope of patent application, in which the polyol component contains an adduct in an amount of 10-40% by weight. 4. For the method of patent application, the polyol component has a warp value of 300 to 700 agiC0H / g. 5. The method as claimed in item 1 of the patent application, wherein the blowing agent is like at least one other gaseous fluorosulfonate compound selected from the group consisting of argon gas fluorine master compounds, hydrogenated fluorocarbon compounds and perfluoro master compounds. 6. For example, the manufacturing method of item 1 of the patent application scope, in which the blowing agent is a mixture of water and at least one other gaseous fluorine master compound, the other gaseous fluorine sulfonate paper scale is applicable to the Chinese National Standard (CNS) A4 specification (210 X 297 gold) 1 H3 compounds are proudly selected from the group consisting of hydrogenated gas carbon compounds, hydrogenated fluorosulfon compounds and total gas sulfon compounds. ?. For example, the manufacturing method of item 1 of the patent application scope, in which the blowing agent is 1,1-digas -1 -fluoroethane. 8. As in the preparation method of item 1 of the patent application scope, the blowing agent is a mixture of water and 1,1-dichloro-1-fluoroethane. 9. For the manufacturing method of item 1 of the patent application scope, 15-40 parts by weight of 1,1-digas-1-fluoroethane and 1.0-3.0 parts by weight of water are used with respect to 100 parts by weight of the polyol component As a foaming agent. 10. As in the preparation method of the first item of patent application, the polyisodonate component is polymethylidene polyphenyl polyisocyanate. 11. A rigid polyurethane foam, a rigid polyurethane foam prepared by reacting an organic polyisocyanate component with a polyol component in the presence of a blowing agent, The polyol component includes the adduct N-CH-CH-N. 1 '/ 2 2 \ (Ε〇)-(ρ〇) of alkylene oxide having the formula -η H- (P〇) m3- (EO) n ^ (EO)-(PO) Ή The Employee Welfare Committee of the Central Bureau of Standards of the Ministry of Economic Affairs printed a base B stretch of ο in which the base B stretch is 3 π and 2 η; the number of flat and average base propylene stretching oxygen is S3 and η + + 1 and the size of this paper are applicable to China National Standards (CNS) A4 specifications (210 X 297 public director) 2
TW83107042A 1993-08-06 1994-08-02 TW311920B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19619193 1993-08-06

Publications (1)

Publication Number Publication Date
TW311920B true TW311920B (en) 1997-08-01

Family

ID=16353711

Family Applications (1)

Application Number Title Priority Date Filing Date
TW83107042A TW311920B (en) 1993-08-06 1994-08-02

Country Status (2)

Country Link
CN (1) CN1056857C (en)
TW (1) TW311920B (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DD210540A3 (en) * 1982-04-26 1984-06-13 Mo Aviatsionnyj I Im S Ordzhon STEP-BY-STEP BIOCHEMICAL CLEANING OF REMOVAL OF PHENOL COMPOUNDS
GB8516826D0 (en) * 1985-07-03 1985-08-07 Dow Chemical Nederland Precursor compositions of nitrogen-containing polyols
US4704410A (en) * 1986-06-30 1987-11-03 The Dow Chemical Company Molded rigid polyurethane foams prepared from aminoalkylpiperazine-initiated polyols

Also Published As

Publication number Publication date
CN1099765A (en) 1995-03-08
CN1056857C (en) 2000-09-27

Similar Documents

Publication Publication Date Title
TWI296630B (en) Process for the production of flexible polyurethane foams
CZ156599A3 (en) Solid polyurethane foams
NO151313B (en) PROCEDURE AND DEVICE FOR IDENTIFICATION AND SORTING OF METAL BOXES
US6846850B2 (en) Rigid polyurethane foams with improved properties
EP0477920B2 (en) Process for preparing articles of polyurethane foams
JPH11513716A (en) Rigid polyurethane foam
US20050070619A1 (en) Blowing agent enhancers for polyurethane foam production
TW311920B (en)
NZ234512A (en) Polyols prepared by adding alkylene oxide onto a compound containing at least one ester and/or amide linkage; polyurethane resins and foams prepared therefrom
TW426696B (en) Rigid polyurethane foams
JPH08501345A (en) Polyurethane foam with improved heat insulation and method for producing the same
CA2486667A1 (en) Rigid polyurethane foams for insulation and process for producing same
US4904707A (en) Novel polyol composition and the use thereof in the preparation of rigid polyurethane foams
US3888803A (en) High temperature polyurethane foams
JPH0797429A (en) New polyol composition and production of rigid polyurethane foam by using same
TW422739B (en) Azeotropic compositions of perfluorohexane, or 1,1,1,4,4,4-hexafluorobutane, or 1,3-dioxolane and hydrocarbons having 5 or 6 carbon atoms and the use thereof in the production of foams
US5198475A (en) Polyol and utilization thereof
US7300961B2 (en) Polyol compositions useful for preparing dimensionally stable, low density water-blown rigid foams and the processes related thereto
EP0483431B1 (en) Polyol and utilization thereof
CN102093589B (en) Foaming agent composition, polyurethane hard foamed plastic and manufacturing method thereof
TW387912B (en) A process for preparing hydrocarbon-blown polyurethane rigid foams
JPH03258822A (en) Preparation of rigid polyurethane foam
JPH03258824A (en) Preparation of rigid polyurethane foam
JPH0393827A (en) Production of rigid polyurethane foam
JPH02255818A (en) Polyol composition for rigid urethane foam