CN1083462C - 制备软聚氨酯泡沫塑料的方法 - Google Patents

制备软聚氨酯泡沫塑料的方法 Download PDF

Info

Publication number
CN1083462C
CN1083462C CN98114781A CN98114781A CN1083462C CN 1083462 C CN1083462 C CN 1083462C CN 98114781 A CN98114781 A CN 98114781A CN 98114781 A CN98114781 A CN 98114781A CN 1083462 C CN1083462 C CN 1083462C
Authority
CN
China
Prior art keywords
weight
polyvalent alcohol
ethylene oxide
hydroxy functionality
polyoxyalkylene polyol
Prior art date
Legal status (The legal status 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 status listed.)
Expired - Fee Related
Application number
CN98114781A
Other languages
English (en)
Other versions
CN1215066A (zh
Inventor
G·布莱斯
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hentzman ICI Chemical Product Co., Ltd.
Original Assignee
HENTZMAN ICI CHEMICAL PRODUCT 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
Family has litigation
First worldwide family litigation filed litigation Critical https://patents.darts-ip.com/?family=10706387&utm_source=google_patent&utm_medium=platform_link&utm_campaign=public_patent_search&patent=CN1083462(C) "Global patent litigation dataset” by Darts-ip is licensed under a Creative Commons Attribution 4.0 International License.
Application filed by HENTZMAN ICI CHEMICAL PRODUCT CO Ltd filed Critical HENTZMAN ICI CHEMICAL PRODUCT CO Ltd
Publication of CN1215066A publication Critical patent/CN1215066A/zh
Application granted granted Critical
Publication of CN1083462C publication Critical patent/CN1083462C/zh
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40—High-molecular-weight compounds
    • C08G18/48—Polyethers
    • C08G18/4804—Two or more polyethers of different physical or chemical nature
    • C08G18/4816—Two or more polyethers of different physical or chemical nature mixtures of two or more polyetherpolyols having at least three hydroxy groups
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40—High-molecular-weight compounds
    • C08G18/48—Polyethers
    • C08G18/4804—Two or more polyethers of different physical or chemical nature
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2110/00—Foam properties
    • C08G2110/0008—Foam properties flexible
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2110/00—Foam properties
    • C08G2110/0041—Foam properties having specified density
    • C08G2110/005—< 50kg/m3
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2110/00—Foam properties
    • C08G2110/0041—Foam properties having specified density
    • C08G2110/0058—≥50 and <150kg/m3
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G2110/00—Foam properties
    • C08G2110/0083—Foam properties prepared using water as the sole blowing agent
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S521/00—Synthetic resins or natural rubbers -- part of the class 520 series
    • Y10S521/914—Polyurethane cellular product formed from a polyol which has been derived from at least two 1,2 epoxides as reactants

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polyurethanes Or Polyureas (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

一种制备软聚氨酯泡沫塑料的方法，此方法是将聚异氰酸酯与至少两种多元醇反应，这两种多元醇合起来的平均标称羟基官能度为2.5至6，第一种多元醇用量是两种多元醇总重的5-30重量%，且第一种多元醇是聚氧化烯多元醇，其平均标称羟基官能度至少为4，平均羟基当量为100-1500，且氧化乙烯含量至少为50重量%，第二种多元醇是另一种多元醇，其用量是两种多元醇总量的95-70重量%；和使用发泡剂。

Description

制备软聚氨酯泡沫塑料的方法
本发明涉及用来制造聚酯软泡沫塑料的多元醇组合物以及所述泡沫塑料的制造方法。
将有机聚异氰酸酯如甲苯二异氰酸酯(TDI)或二苯基甲烷二异氰酸酯(MDI)与聚醚多元醇以及发泡剂一起反应制备聚氨酯软泡沫塑料的方法已相当成熟。聚醚通常是由氧化丙烯得出的聚氧化丙烯多元醇或是由氧化丙烯和氧化乙烯的各种组合得出的聚(氧化丙烯一氧化乙烯)多元醇。氧化乙烯封端的聚氧化丙烯多元醇类中，氧化烯基只占总氧化烯残系物的极小部分，由于它们对异氰酸酯有较高的反应性，从而特别重要。氧化乙烯含量较高的多元醇，例如含50％(重量)或更多氧化己烯的多元醇通常作为微量添加物使用，以确保泡沫塑料具有开孔结构。软泡沫塑料制备中最常用的多元醇是二元醇和三元醇。
业已发现，具有包括极好回弹性的有价值的性能的软泡沫塑料可由包含具有相对较高氧化己烯含量的一定量高官能度多元醇的多元醇组合物来制备。
因此，本发明提供一种多元醇组合物，其平均标称羟基官能度为2.5-6，该组合物包含：
(a)5-30重量％的聚氧化烯多元醇，其平均标称羟基官能度至少为4，平均羟基当量为100-1500，最好为100-1000，且氧化己烯含量至少为50重量％，和
(b)95-70重量％另一种多元醇。
 此处“平均标称羟基官能度”是指在假设聚氧化烯多元醇的平均官能度与制备过程中所用的引发剂的平均官能度(每个分子中活性氢的数目)相同——尽管实际上由于终端不饱和常常较少——的条件下，多元醇组合物的平均官能度(每个分子中羟基的数目)。
具有组分(a)所需特性的聚氧化烯多元醇是本领域公知的，并且可按常规方法制得，即，将氧化乙烯，或者氧化乙烯和氧化丙烯同时和/或以任意顺序，与带有至少四个活性氢原子的引发剂(例如：多元醇、多元胺等)反应。
多元醇组分(b)以平均标称羟基官能度是2-6(尤其是2-4)为宜，平均羟基当量以1000-3000为宜，并且可以选自用于聚氨酯制造中公知的任何一类多元醇，例如：聚酯、聚酯酰胺、聚硫醚、聚碳酸酯、聚缩醛、聚烯烃和聚硅氧烷。但是，组分(b)最好是与组分(b)的官能度和/或氧化乙烯含量不同的聚氧化烯多元醇，例如：组分(b)可以是氧化烯含量低于50重量％(一般低于20重量％)的聚氧化烯三元醇。
优选的多元醇组合物含有至少6重量％，较好至少6重量％至低于20重量％，最好至少10重量％至低于20重量％的组分(a)。此外，构成组分(a)的聚氧化烯多元醇最好具有至少下列特性之一：
(i)平均标称羟基官能度大小4，例如6；
(ii)氧化乙烯含量至少为70重量％，例如90-100重量％。必要时，聚氧化烯多元醇(或当使用其混合物时，一种或多种聚氧化烯多元醇)可含有分散的聚合物颗粒。这样的聚合物改性多元醇在先有技术中已有详尽描述，它还包括在聚氧化烯多元醇中，一种或多种乙烯基单体(例如乙腈和苯乙烯)原位聚合得到的产物，或在聚氧化烯多元醇中，聚异氰酸酯与氨基或羟基官能化合物原位反应得到的产物。
上述多元醇组合物在制造软聚氨酯泡沫塑料中，特别是回弹性数值(ISO 8307测得)至少为55％，最好至少为58％的泡沫塑料中具有特别价值。
从而，本发明的又一方面是提供制备软聚氨酯泡沫塑料的方法，即，在发泡剂存在下，将聚异氰酸酯与至少两种多元醇反应，这两种多元醇合起来的平均标称羟基官能度为2.5至6，第一种多元醇用量是两种多元醇总重的5-30重量％，且第一种多元醇是聚氧化烯多元醇，其平均标称羟基官能度至少为4，平均羟基当量为100-1500，且氧化乙烯含量至少为50重量％，第二种多元醇是另一种多元醇，其用量是两种多元醇总量的95-70重量％。
可用来制备软泡沫塑料的有机聚异氰酸酯包括脂肪族、环脂族和芳脂族聚异氰酸酯，尤其是芳香族聚异氰酸酯，例如二异氰酸甲苯酯(TDI)和二苯基甲烷二异氰酸酯(MDI)通常用于软泡沫塑料的制造。
优选的聚异氰酸酯是二苯基甲烷二异氰酸酯组合物，尤其是正常室温下为液体的组合物。因此，适当的聚异氰酸酯包括MDI异构体的液体混合物，尤其是包含4，4′-异构体以及不超过60％的2，4′-异构体和不超过5％的2，2-异构体的混合物，上述组合含量均以占总组合物重量的百分数表示。
其它可用的二苯基甲烷二异氰酸酯包括由聚亚甲基聚亚苯基聚异氰酸酯构成的或包含它的组合物。从而，可使用这样的混合物：它含至少70重量％纯MDI(4，4′-异构体或异构体混合物)和不超过30重量％的所谓聚合MDI，聚合MDI含有25-65重量％的二异氰酸酯，其余主要是异氰酸酯官能度大于2的聚亚甲基聚亚苯基聚异氰酸酯。也可使用纯MDI与含有较多(直至100％)所述高官能度聚异氰酸酯的聚合MDI组合物的混合物。
其它可用的MDI组合物包括改性形式的MDI，也就是说，以已知方法通过引入例如：氨基甲酸乙酯、脲基甲酸酯、脲、缩二脲、碳化二亚胺、uretonimine或异氰脲酸酯残基将MDI改性。其它可用的MDI的改性形式包括例如EP-A-0103996所述的聚脲在MDI中的分散体。
还有一类可用的二苯基甲烷二异氰酸酯组合物包括上述的MDI异构体、异构体混合物、聚合MDI、改性MDI等和不超过20重量％的另一种聚异氰酸酯或聚异氰酸酯混合物。其它可与MDI混合使用的聚异氰酸酯包括脂肪族、环脂族和芳脂族聚异氰酸酯，特别是二异氰酸酯，例如六亚甲基二异氰酸酯、异佛尔酮二异氰酸酯、环己烷-1，4-二异氰酸酯、4，4′-二环已基甲烷二异氰酸酯和间和对四甲基二甲苯二异氨酸酯特别是芳香族聚异氰酸酯，例如甲苯二异氰酸酯和苯二异氰酸酯。
本发明方法优选的发泡剂是水，还可同时使用物理发泡剂，例如低沸点有机氟化合物。发泡剂的用量可按已知的方式变化，以达到预期的泡沫密度，例如：水的适当用量以多元醇组合物重量为基准计是0.25-20重量％，优选0.25-10重量％，最佳是0.25重量％至5重量％以下。最好只用水作发泡剂。考虑到多元醇组合物、水和任何其它异氰酸酯反应性物质(例如：链扩展剂或交联剂)，反应体系的均异氨酸酯指数可低至10或高至120。
发泡反应混合物可包含一种或多种该反应混合物常用的添加剂。所述添加剂包括催化剂，例如叔胺和锡化合物；表面活性剂和泡沫稳定剂，例如硅氧烷一氧化烯共聚物；链扩展剂，例如低分子量二元醇或二元胺；交联剂，例如三乙醇胺；阻燃剂；有机和无机填料；颜料；抑制所谓沸腾发泡效应(boiling-foam effect)的物质，例如聚二甲基硅氧烷；和内部脱模剂。
从而，在又一方面，本发明提供的反应体系包括：
(i)聚异氰酸酯组分；
(ii)平均标称羟基官能度为2.5-6的多元醇组合物，它包括：
(a)5-30重量％的聚氧化烯多元醇，其平均标称羟基官能度至少为4；平均羟基当量为100-1500，氧化乙烯含量至少为50重量％
(b) 95-70重量％的另一种多元醇；
(iii)一种发泡剂，包括：水，和可选的
(iv)一种或多种泡沫塑料配方中常用的添加剂。这样的反应体系最好用于制造软泡沫塑料。术语“反应体系”定义为各组分的一种组合，其中聚异氰酸酯组分装在一容器中，与异氰酸酯反应性组分分开。
在实施本发明方法时，可采用公知的一步法、半预聚体工艺或全预聚体工艺，同时采用常用的混合设备，泡沫塑料可制成块料或模塑等形式。当采用预聚体工艺时，两种多元醇的每一种都可单独或混合使用，与聚异氰酸酯预反应。前述用量的计算是基于预聚体中多元醇和多元醇组合物中多元醇的。
本发明用下列实施例说明，但并不局限于此。其中全部份数、百分数和比率均以重量计。
下列术语表用来说明实施例中未说明的反应成分。
术语表
F2805是Daltocel F2805，一种氧化乙烯封端的聚氧化丙烯三元醇，其氧化乙烯含量为15％，分子量为6000，由Imperial ChemicalInduatries PLC购得。Daltocel是ICI的商标。
G2005是Atlas G2005，一种分子量为1800的聚氧化乙烯六元醇，从Imperical Chemical Industries PLC.购得。
A2580是Arcol2580，一种具有无规氧化乙烯和氧化丙烯残基且氧化乙烯含量为77％的聚醚三元醇，其分子量为4000，从Arco购得。
PolyolX是EO含量为15重量％且OHv＝160的六官能团多元醇。
PolyolY是EO含量为15重量％且OHv＝91的六官能团多元醇。
PolyolZ是EO含量为75重量％且OHv＝41的六官能团多元醇。
PBA2185是NCO含量为30.7％的聚合MDI，从Imperial ChemicalIndustries PLC购得。
预聚体A的NCO含量为6％，通过将75pbw的OH值＝36的三元醇(13％EO-封端)与25pbw MDI(10％2，2′+2，4′)反应获得。
Niax A1：催化剂，可从Union Carbide得到。
Dabco 33LV：催化剂，可从Air Products得到。
Dabco EG：催化剂，可从Air Products得到。
Dabco 80/20：催化剂，可从Air Products得到。
B4113是Tegostab B4113，一种硅酮表面活性剂，可从GoldshmidtAG得到。Tegostab是Goldschmidt的商标。
回弹率按ISO8307测定，CL 40％和滞后损失按ISO 3386-I测定。CLD 40％是在40％压缩下的压缩载荷挠度。
实施例1
将表I给出的配方台式混合，制得软泡沫塑料，数量均为重量份。表1也给出了所得泡沫塑料的性质。
                   表1对比实施例：A2580(三元醇)实验          1     2     3     4     5预聚体      A 90    90    90    90    90PBA2185       10    10    10    10    1033LV          0.8   0.8   0.8   0.8   0.8Niax A1       0.1   0.1   0.1   0.1   0.1A2580         0     2     4     6     10水            1.8   1.8   1.8   1.8   1.8指数          100   99    98    98    96密度i         51    56    57    55    58kg/m3CLD 40％，    3.4   4.1   3.5   4.8   3.7kPa滞后损失，    29    22    18    19    16％回弹率，      49    54    54    52    45％
                  表1(续)实施例：G2005：六官能团多元醇实验        6     7     8     9     10预聚体    A 90    90    90    90    90PBA2185     10    10    10    10    1033LV        0.8   0.8   0.8   0.8   0.8Niax A1     0.1   0.1   0.1   0.1   0.1G2005       0     2     4     6     10水          1.8   1.8   1.8   1.8   1.8指数：      100   100   100   100   100密度        51    56    60    61    62kg/m3CLD 40％，  3.4   4.5   4.6   4.4   3.5kPa滞后损失，  29    23    19    18    15％回弹率，    49    52    54    59    60％
实施例2
软泡沫塑料是通过将聚异氰酸酯与含有高含量氧化乙烯的聚醚六元醇的反应混合物反应而制得。表2给出配方(重量份)和泡沫塑料性质。
               表2实验        1     2     3     4F2805       100   95    90    85G2005       0     5     10    15Niax A1     0.1   0.1   0.1   0.1Dabco 33LV  0.5   0.5   0.5   0.5B4113       0.5   0.5   0.5   0.5水          3     3     3     3PBA 2185    46    47    49    50指数        90    89    90    90密度        46    56    57    61kg/m3回弹率      54    61    65    70％CLD 40％    3.5   6.1   4.7   3.8kPa滞后损失    27    22    17    15％
实施例3
由表3所示的各组分(重量份)制得了数种其它的软泡沫塑料。示有★符号者为对比试验。
                                         表3实 验       1★    2★    3★    4★    5★    6     7     8     9★     10★   11★F 2805      50    95    90    95    90    95    90    85    100    95    85G 2005      50    -     -     -     -     -     -     -     -      -     -Polyol X    -     5     10    -     -     -     -     -     -      -     -Polyol Y    -     -     -     5     10    -     -     -     -      -     -Polyol Z    -     -     -     -     -     5     10    15    0      5     15Niax A1     -     0.1   0.1   0.1   0.1   0.1   0.1   0.1   -      -     -Dabco 33LV  -     0.5   0.5   0.5   0.5   0.5   0.5   0.5   1.5    1.5   2.5Dabco EG    0.4   -     -     -     -     -     -     -     -      -     -Dabco 80/20 0.2   -     -     -     -     -     -     -     -      -     -水          3     3     3     3     3     3     3     3     10     10    10PBA2185        72.2  48.5  50.5  47.9  48.6  47.3  47.5  47.7  47.5   47.5  47.5指数        100   90    90    90    90    90    90    90    30     30    30自由起发密度
        -     39.5  38.7  42.5  40.1  43.5  41.7  40.8  31.5   34.9  49.9Kg/m3回弹率％          -     49    40    52    48    64    68    69    35     37    50CLD，40％，kPa         -     3.7   4.7   3.9   3.8   3.2   2.6   2.5   2.5    2.5   3.2
注：实验1中，泡沫塑料瘪泡。

Claims (11)

1.一种制备软聚氨酯泡沫塑料的方法，此方法是将聚异氰酸酯与至少两种多元醇反应，这两种多元醇合起来的平均标称羟基官能度为2.5至6，第一种多元醇用量是两种多元醇总重的5-30重量％，且第一种多元醇是聚氧化烯多元醇，其平均标称羟基官能度至少为4，平均羟基当量为100-1500，且氧化乙烯含量至少为50重量％，第二种多元醇是另一种多元醇，其用量是两种多元醇总量的95-70重量％；和使用包括水的发泡剂，其用量按所述至少两种多元醇的重量计为0.25-10重量％。
2.按权利要求1的方法，其中聚异氰酸酯组分包含二苯基甲烷二异氰酸酯。
3.按权利要求1或2的方法，其中发泡剂包括水，还可同时使用物理发泡剂。
4.按权利要求1或2的方法，其中所述第二种多元醇包含聚氧化烯多元醇，其平均标称羟基官能度为2-6，平均羟基当量为1000-3000，且氧化乙烯含量低于50重量％。
5.按权利要求1或2的方法，其中聚氧化烯多元醇的平均标称羟基官能度为2-4，且氧化乙烯含量低于20重量％。
6.按权利要求1或2的方法，包含至少6重量％至20重量％以下的第一种多元醇。
7.按权利要求1或2的方法，其中所述第一种多元醇包含平均标称羟基官能度大于4的聚氧化烯多元醇。
8.按权利要求1或2的方法，其中所述第一种多元醇包含氧化乙烯含量至少为70重量％的聚氧化烯多元醇。
9.按权利要求1或2的方法，其中聚氧化烯多元醇的氧化乙烯含量为90-100重量％。
10.按权利要求1或2的方法，其中水含量基于至少该两种多元醇的重量计为0.25重量％至5重量％以下。
11.一种反应体系，它包括：
(i)一种聚异氰酸酯；
(ii)一种多元醇组合物，其平均标称羟基官能度为2.5-6，该组合物包含：
(a)5-30重量％的聚氧化烯多元醇，其平均标称羟基官能度至少为4，平均羟基当量为100-1500，且氧化乙烯含量至少为50重量％，和
(b)95-70重量％的另一种多元醇；
(iii)一种包括水的发泡剂，其用量按多元醇组合物计为0.25-10重量％；以及可选的
(iv)一种或多种泡沫塑料配方中常用的添加剂。
CN98114781A 1991-12-17 1998-06-15 制备软聚氨酯泡沫塑料的方法 Expired - Fee Related CN1083462C (zh)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB919126740A GB9126740D0 (en) 1991-12-17 1991-12-17 Polyol compositions
GB9126740.1 1991-12-17

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
CN92114553A Division CN1042232C (zh) 1991-12-17 1992-12-17 多元醇组合物

Publications (2)

Publication Number Publication Date
CN1215066A CN1215066A (zh) 1999-04-28
CN1083462C true CN1083462C (zh) 2002-04-24

Family

ID=10706387

Family Applications (2)

Application Number Title Priority Date Filing Date
CN92114553A Expired - Fee Related CN1042232C (zh) 1991-12-17 1992-12-17 多元醇组合物
CN98114781A Expired - Fee Related CN1083462C (zh) 1991-12-17 1998-06-15 制备软聚氨酯泡沫塑料的方法

Family Applications Before (1)

Application Number Title Priority Date Filing Date
CN92114553A Expired - Fee Related CN1042232C (zh) 1991-12-17 1992-12-17 多元醇组合物

Country Status (11)

Country Link
US (1) US5521226A (zh)
EP (1) EP0547764B1 (zh)
JP (1) JP3308612B2 (zh)
KR (1) KR100251337B1 (zh)
CN (2) CN1042232C (zh)
AU (1) AU654593B2 (zh)
CA (1) CA2084809A1 (zh)
DE (1) DE69221274T2 (zh)
ES (1) ES2104852T3 (zh)
GB (1) GB9126740D0 (zh)
ZA (1) ZA929105B (zh)

Families Citing this family (60)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4204395A1 (de) * 1992-02-14 1993-08-19 Bayer Ag Verfahren zur herstellung von kalthaertenden polyurethan-weichformschaumstoffen
JPH0790045A (ja) * 1993-05-11 1995-04-04 Sanyo Chem Ind Ltd 軟質ポリウレタンフォームの製法
US5382272A (en) * 1993-09-03 1995-01-17 Rodel, Inc. Activated polishing compositions
GB9325043D0 (en) * 1993-12-07 1994-02-02 Polyol Int Bv Polyol compositions and their use in the preparation of high resilience polyurethane foams
DE19508079A1 (de) * 1995-03-08 1996-09-12 Bayer Ag Verfahren zur Herstellung von hochelastischen Polyurethanschaumstoffen
DE19610262A1 (de) * 1996-03-15 1997-09-18 Bayer Ag Verfahren zur Herstellung Kohlenwasserstoff-getriebener Polyurethan-Hartschaumstoffe
DE19621305A1 (de) * 1996-05-28 1997-12-04 Bayer Ag Verfahren zur Herstellung von elastischen Polyurethanblockschaumstoffen
DE19725020C2 (de) * 1997-06-13 2001-10-31 Bayer Ag Verfahren zur Herstellung elastischer Polyurethanweichschaumstoffe
DE19736976A1 (de) * 1997-08-25 1999-03-04 Basf Ag Verfahren zur Herstellung von Polyurethanweichschaumstoffen
CN1117111C (zh) * 1997-09-26 2003-08-06 陶氏环球技术公司 高使用温度的聚氨酯弹性体
US5874485A (en) * 1997-11-10 1999-02-23 Bayer Corporation Flexible foams and flexible molded foams based on allophanate-modified diphenylmethane diisocyanates and processes for the production of these foams
US5821275A (en) * 1997-11-10 1998-10-13 Bayer Corporation Flexible foams and flexible molded foams based on liquid isocyanate-terminated allophanate-modified MDI prepolymer blends and processes for the production of these foams
TW568921B (en) 1998-08-07 2004-01-01 Huntsman Int Llc Process for preparing a moulded flexible polyurethane foam
JP3181280B2 (ja) * 1999-09-03 2001-07-03 東洋ゴム工業株式会社 シートクッションパッド
CN1175020C (zh) * 1999-11-02 2004-11-10 亨茨曼国际有限公司 制造粘弹泡沫塑料、混合多元醇的方法以及对此有用的反应体系
WO2001032735A1 (en) * 1999-11-02 2001-05-10 Huntsman International Llc Process for making high resilience foams
EP1252215B1 (en) * 2000-01-17 2005-05-04 Huntsman International Llc Process for preparing a free rise or slabstock flexible polyurethane foam
CA2396845C (en) * 2000-02-14 2009-04-14 Huntsman International Llc Process for preparing a flexible polyurethane foam
US6271279B1 (en) 2000-07-10 2001-08-07 Bayer Corporation High resilient flexible urethane foam and flexible molded foams based on allophanate modified isocyanates
EP1172387A1 (en) * 2000-07-14 2002-01-16 Huntsman International Llc Process for preparing an elastomer
EP1174453A1 (en) * 2000-07-17 2002-01-23 Huntsman International Llc Process for preparing a flexible polyurethane foam
EP1178061A1 (en) * 2000-08-01 2002-02-06 Huntsman International Llc Process for preparing a polyurethane material
DE10105558A1 (de) * 2001-02-06 2005-04-07 Basf Ag Verfahren zur Herstellung von in-situ retikulierten Polyurethanweichschaumstoffen
DE10105559A1 (de) * 2001-02-06 2002-08-08 Basf Ag Verfahren zur Herstellung von niedrigdichten hydrophilen Polyurethanweichschaumstoffen
DE10105560A1 (de) * 2001-02-06 2002-08-08 Basf Ag Verfahren zur Herstellung von Polyurethanweichschäumen
DE10105557A1 (de) * 2001-02-06 2002-08-08 Basf Ag Verfahren zur Herstellung von geruchsarmen Polyurethanweichschaumstoffen
US6372812B1 (en) 2001-02-20 2002-04-16 Foamex L.P. Higher support, lower density cushioning foams
EP1234843A1 (en) * 2001-02-26 2002-08-28 Huntsman International Llc Process for preparing a flexible polyurethane foam
US6710096B2 (en) 2002-07-22 2004-03-23 Basf Corporation Polyether polyol for foam applications
US20050131095A1 (en) * 2002-08-02 2005-06-16 Jianming Yu Novel polyols
EP1527114B1 (en) * 2002-08-02 2007-10-17 Huntsman International Llc Prepolymer, polyol composition and process for making a flexible foam
US6740687B2 (en) * 2002-08-14 2004-05-25 Foamex L.P. Latex replacement polyurethane foams with improved flame retardancy
CA2441246A1 (en) * 2002-09-23 2004-03-23 Hilti Aktiengesellschaft Two-component foam system for producing constructional foams and their use
ITRM20020471A1 (it) * 2002-09-24 2004-03-25 Adler Plastic S P A Composizione poliuretanica fonoassorbente e fonoisolante.
US6716890B1 (en) 2003-01-30 2004-04-06 Foamex L.P. Polyurethane foams with fine cell size
US6797736B1 (en) * 2003-03-19 2004-09-28 Basf Corporation Method of forming high resilience slabstock polyurethane foam
US20050038132A1 (en) * 2003-03-19 2005-02-17 Raghuram Gummaraju Composition for forming a foamed article and an article of furniture having the foamed article disposed therein
US6784218B1 (en) * 2003-03-19 2004-08-31 Basf Corporation Method of forming high resilience slabstock polyurethane foam displaying latex-like characteristics
DE10314762A1 (de) † 2003-03-31 2004-10-14 Basf Ag Verfahren zur Herstellung von Polyurethan-Weichschaumstoffen
US7238730B2 (en) * 2003-06-26 2007-07-03 Basf Corporation Viscoelastic polyurethane foam
US7208531B2 (en) * 2003-06-26 2007-04-24 Basf Corporation Viscoelastic polyurethane foam
FR2858328B1 (fr) * 2003-08-01 2008-01-04 Saint Gobain Performance Plast Mousse de polyurethanne, procede de fabrication et utilisation
JP4666278B2 (ja) * 2004-02-13 2011-04-06 日本ポリウレタン工業株式会社 高通気性・低反発弾性のポリウレタンフォームの製造方法。
US8165281B2 (en) * 2004-07-28 2012-04-24 At&T Intellectual Property I, L.P. Method and system for mapping caller information to call center agent transactions
US7326738B2 (en) 2004-07-29 2008-02-05 Basf Corporation Composition and process for forming a flexible polyurethane foam sealing device
US20060029788A1 (en) * 2004-08-04 2006-02-09 Foamex L.P. Lower density, thermoformable, sound absorbing polyurethane foams
US20090012195A1 (en) * 2007-07-05 2009-01-08 Neff Raymond A Resin composition for use in forming a polyurethane article with increased comfort
JP5756012B2 (ja) * 2008-07-18 2015-07-29 ダウ グローバル テクノロジーズ エルエルシー 天然資源を基質とする粘弾性発泡体
US8901187B1 (en) 2008-12-19 2014-12-02 Hickory Springs Manufacturing Company High resilience flexible polyurethane foam using MDI
US20100160470A1 (en) * 2008-12-23 2010-06-24 Smiecinski Theodore M Flexible Polyurethane Foam
US8604094B2 (en) 2008-12-23 2013-12-10 Basf Se Flexible polyurethane foam and method of producing same
US8906975B1 (en) 2009-02-09 2014-12-09 Hickory Springs Manufacturing Company Conventional flexible polyurethane foam using MDI
JP4920051B2 (ja) * 2009-02-25 2012-04-18 株式会社日立製作所 酸素燃焼ボイラプラント及び酸素燃焼ボイラプラントの運転方法
KR101746885B1 (ko) 2009-10-07 2017-06-14 헌트스만 인터내셔날, 엘엘씨 가요성 폴리우레탄 발포체의 제조 방법
CN103282398B (zh) 2010-11-03 2015-02-18 陶氏环球技术有限责任公司 自冲压的聚氨酯体系
CN103635503B (zh) 2011-02-14 2016-03-09 陶氏巴西东南工业有限公司 低密度聚氨酯泡沫体
JP6010608B2 (ja) * 2012-03-29 2016-10-19 株式会社ブリヂストン シートパッド用ポリウレタンフォーム
US20150141542A1 (en) * 2012-05-22 2015-05-21 Bayer Materialscience Ag Method for producing flame-protected polyurethane foams having low bulk densities
AU2013329491A1 (en) * 2012-10-10 2015-04-30 Basf Se Viscoelastic polyurethane foam
CN106084749A (zh) * 2016-06-16 2016-11-09 江苏新光环保工程有限公司 一种聚氨酯吸声材料及其制备方法

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2140227A1 (zh) * 1971-06-03 1973-01-12 Bayer Ag
EP0263280A1 (de) * 1986-09-05 1988-04-13 Bayer Ag Verfahren zur Herstellung von elastischen, offenzelligen Polyurethan-Weichschaumstoffen mit erhöhter Stauchhärte
EP0296449A1 (de) * 1987-06-26 1988-12-28 Bayer Ag Verfahren zur Herstellung von kalthärtenden Polyurethan-Weichformschaumstoffen
EP0404441A1 (en) * 1989-06-21 1990-12-27 Imperial Chemical Industries Plc Isocyanate-reactive compositions

Family Cites Families (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3509077A (en) * 1966-07-07 1970-04-28 Allied Chem Rigid polyurethane foams from certain polyether mixtures
US3857800A (en) * 1970-06-19 1974-12-31 Dunlop Holdings Ltd Flexible polyurethane foams prepared from a mixture of polyether polyols
IT1058454B (it) * 1976-03-17 1982-04-10 Montedison Spa Tprcedimento per la produzione di schiume poliuretaniche soffici ed extra supersoffici
JPS5566917A (en) * 1978-11-14 1980-05-20 Toyo Tire & Rubber Co Ltd Manufacture of non-yellowing integral polyurethane foam
EP0103996B1 (en) * 1982-09-17 1988-09-21 Imperial Chemical Industries Plc Polyurea dispersions in organic isocyanates
DE3402310A1 (de) * 1984-01-24 1985-07-25 Bayer Ag, 5090 Leverkusen Harte, geschlossenzellige, flammfeste polyurethanschaumstoffe
JPS6257467A (ja) * 1985-09-06 1987-03-13 Asahi Glass Co Ltd コ−テイング剤組成物
DE3806476A1 (de) * 1988-03-01 1989-09-14 Bayer Ag Verfahren zur herstellung von kalthaertenden polyurethan-weichformschaumstoffen mit hervorragenden daempfungseigenschaften
US4929646A (en) * 1988-04-26 1990-05-29 The Dow Chemical Company Polyurethane foam prepared using high functionality cell openers
DE3903100A1 (de) * 1989-02-02 1990-08-23 Bayer Ag Verfahren zur herstellung von elastischen und offenzelligen polyurethan-weichformschaumstoffen
US5001167A (en) * 1989-03-21 1991-03-19 The Dow Chemical Company Solvent resistant polyetherpolyurethane products
JPH0733423B2 (ja) * 1989-10-03 1995-04-12 日本ポリウレタン工業株式会社 軟質ポリウレタン発泡体の製造方法
DE3942329A1 (de) * 1989-12-21 1991-06-27 Basf Ag Verfahren zur herstellung von polyurethan-weichschaumstoffen mit geringer stauchhaerte und hierfuer verwendbare blockpolyoxypropylen-polyoxyethylen-polyolgemische
DE3942330A1 (de) * 1989-12-21 1991-06-27 Basf Ag Verfahren zur herstellung von flexiblen polyurethan-weichschaumstoffen mit viskoelastischen, koerperschalldaempfenden eigenschaften und hierzu verwendbare polyoxyalkylen-polyol-mischungen
JPH03199223A (ja) * 1989-12-27 1991-08-30 Achilles Corp クッション材用ポリウレタンフォーム
DE59207922D1 (de) * 1991-05-03 1997-03-06 Ciba Geigy Ag Polyolkomponente für die Herstellung von Polyurethanformkörpern
GB9126741D0 (en) * 1991-12-17 1992-02-12 Ici Plc Polyurethane foams

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2140227A1 (zh) * 1971-06-03 1973-01-12 Bayer Ag
EP0263280A1 (de) * 1986-09-05 1988-04-13 Bayer Ag Verfahren zur Herstellung von elastischen, offenzelligen Polyurethan-Weichschaumstoffen mit erhöhter Stauchhärte
EP0296449A1 (de) * 1987-06-26 1988-12-28 Bayer Ag Verfahren zur Herstellung von kalthärtenden Polyurethan-Weichformschaumstoffen
EP0404441A1 (en) * 1989-06-21 1990-12-27 Imperial Chemical Industries Plc Isocyanate-reactive compositions

Also Published As

Publication number Publication date
AU2857092A (en) 1993-06-24
CN1042232C (zh) 1999-02-24
KR930012851A (ko) 1993-07-21
US5521226A (en) 1996-05-28
CN1073690A (zh) 1993-06-30
DE69221274T2 (de) 1997-12-04
JP3308612B2 (ja) 2002-07-29
CN1215066A (zh) 1999-04-28
EP0547764B1 (en) 1997-07-30
GB9126740D0 (en) 1992-02-12
AU654593B2 (en) 1994-11-10
KR100251337B1 (ko) 2000-04-15
CA2084809A1 (en) 1993-06-18
EP0547764A1 (en) 1993-06-23
ZA929105B (en) 1994-05-05
DE69221274D1 (de) 1997-09-04
ES2104852T3 (es) 1997-10-16
JPH05262844A (ja) 1993-10-12

Similar Documents

Publication Publication Date Title
CN1083462C (zh) 制备软聚氨酯泡沫塑料的方法
CN1043235C (zh) 聚氨酯泡沫塑料
CN1042231C (zh) 聚氨酯泡沫塑料
CN1070874C (zh) 制备柔性泡沫体的方法
EP0712876B1 (en) Isocyanate composition and process for making flexible foams therefrom
CN1772786B (zh) 具有低堆积密度和压缩强度的软泡沫塑料
US6521674B1 (en) Latex-like flexible polyurethane foam and process for making same
CN1221584C (zh) 软质聚氨酯泡沫材料及其制造方法
CN1038332C (zh) 聚氨基甲酸乙酯泡沫体
EP2723789B1 (en) Polyurethane foam elastomers for high temperature applications
CA2014508A1 (en) Polyisocyanate compositions and their use in the manufacture of polymeric foams
CN1343223A (zh) 制备模塑聚氨酯材料的方法
KR20030097878A (ko) 매우 연질의 폴리우레탄 탄성체
KR19990071778A (ko) 가요성 폴리우레탄 발포체의 제조 방법
CN1044253C (zh) 多异氰酸酯组合物
CA2092577C (en) Process for making flexible foams
JP3937811B2 (ja) 軟質ポリウレタンフォームの製造方法
EP0486034B1 (en) Flexible polyurethane foams and process for preparing them
AU704287B2 (en) A flexible polyurethane foam

Legal Events

Date Code Title Description
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C06 Publication
PB01 Publication
C53 Correction of patent for invention or patent application
COR Change of bibliographic data

Free format text: CORRECT: APPLICANT; FROM: IMPERIAL CHEMICAL CORPORATION TO: HENGCIMAN ICI CHEMICALS LTD.

CP03 Change of name, title or address

Address after: The United States Delaware

Applicant after: Hentzman ICI Chemical Product Co., Ltd.

Address before: London, England, England

Applicant before: Imperial Chemical Industries PLC

C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee
REG Reference to a national code

Ref country code: HK

Ref legal event code: GR

Ref document number: 1058201

Country of ref document: HK