JP2015510012A - 硬質ポリウレタンフォーム、硬質ポリウレタンフォームの製造方法及びポリオール混合物 - Google Patents
硬質ポリウレタンフォーム、硬質ポリウレタンフォームの製造方法及びポリオール混合物 Download PDFInfo
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- JP2015510012A JP2015510012A JP2014559228A JP2014559228A JP2015510012A JP 2015510012 A JP2015510012 A JP 2015510012A JP 2014559228 A JP2014559228 A JP 2014559228A JP 2014559228 A JP2014559228 A JP 2014559228A JP 2015510012 A JP2015510012 A JP 2015510012A
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- polyol
- rigid polyurethane
- polyurethane foam
- Prior art date
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Abstract
Description
A)有機もしくは修飾有機ポリイソシアナートまたはこれらの混合物と、
B)2個以上のイソシアナート反応性水素原子を有する化合物との、
C)場合により他のポリエステルポリオール、
D)場合によりポリエーテルオールポリオール、
E)場合により難燃剤、
F)1種または複数の発泡剤、
G)触媒、および
H)場合により他の助剤および/または添加剤
の存在下での、
反応によって得ることが可能な硬質ポリウレタンフォームであって、
成分B)は、
a1)15から40質量%の、2.5から8の平均官能基数を有する1種または複数のポリオールまたはポリアミンと、
a2)2から30質量%の、1種または複数の脂肪酸および/または脂肪酸モノエステルと、
a3)35から70質量%の、1種または複数の炭素原子2から4個のアルキレンオキシドと
の反応生成物を含む硬質ポリウレタンフォームによって達成されることを見出した。
A)有機もしくは修飾有機ポリイソシアナートまたはこれらの混合物と、
B)1種または複数の上記のポリエーテルエステルポリオールと、
C)場合により他のポリエステルポリオールと、
D)場合によりポリエーテルオールポリオールと、
E)場合により難燃剤と、
F)1種または複数の発泡剤と、
G)触媒と、
H)場合により他の助剤および/または添加剤と
の反応によって硬質ポリウレタンフォームを製造する方法をさらに提供する。
B)1種または複数の上記のポリエーテルエステルポリオール、
C)場合により他のポリエステルポリオール、
D)場合によりポリエーテルポリオール、
E)場合により難燃剤、
F)1種または複数の発泡剤、
G)場合により触媒、および
H)場合により他の助剤および/または添加剤
を含むポリオール混合物を提供する。
25から90質量%のポリエーテルエステルポリオールB)、
0から20質量%の他のポリエステルポリオールC)、
0から35質量%のポリエーテルポリオールD)、
0から30質量%の難燃剤E)、
1から40質量%の発泡剤F)、
0.01から5質量%の触媒G)、
0.01から10質量%の助剤および/または添加剤H)
を含む。
50から85質量%のポリエーテルエステルポリオールB)、
0から10質量%、特に0質量%の他のポリエステルポリオールC)、
0から10質量%、特に0質量%のポリエーテルポリオールD)、
0から15質量%の難燃剤E)、
1から30質量%の発泡剤F)、
0.05から3質量%の触媒G)、
0.01から5質量%の助剤および/または添加剤H)
を含むことがより好ましい。
実施例
250.1gのグリセロール、2.5gのイミダゾール、1139.7gのスクロースならびに750.6gのオレイン酸を、最初に25℃で5Lの反応器に投入した。次いで反応器を窒素で不活性化した。ケトルを130℃に加熱し、2858.1gのプロピレンオキシドを計量供給した。4時間の反応時間に続いて、ケトルを100℃で60分間十分に排気し、次いで25℃まで冷却して、4945gの生成物を得た。
OH価:416.3mgKOH/g
粘度(25℃):7210mPas
酸価:0.08mgKOH/g
水含量:0.016%
995.2gのグリセロール、2.5gのイミダゾール、422.8gのスクロースならびに676.1gのオレイン酸メチルを、最初に25℃で5Lの反応器に投入した。次いで反応器を窒素で不活性化した。ケトル(カマ)を130℃に加熱し、2903.4gのプロピレンオキシドを計量供給した。3時間の反応時間に続いて、ケトルを100℃で60分間十分に排気し、次いで25℃まで冷却して、4904.1gの生成物を得た。
OH価:464.5mgKOH/g
粘度(25℃):783mPas
酸価:0.11mgKOH/g
水含量:0.02%
プロピレンオキシドならびに開始剤として糖とグリセロールの混合物をベースとする、490mgKOH/gのヒドロキシル価を有する、55.65質量部のポリエーテルアルコール1、
プロピレンオキシドおよび開始剤としてエチレンジアミンをベースとする、750mgKOH/gのヒドロキシル価を有する、6質量部のポリエーテルアルコール2、
20質量部のヒマシ油、
15質量部のトリス−2−クロロイソプロピルホスファート(TCPP)、
2質量部のシリコーン泡安定剤(Goldschmidt製Tegostab(登録商標)B8443)、
0.5質量部の、酢酸カリウムの50質量%エチレングリコール溶液、および
0.85質量部の水
から出発して混合することによって、ポリオール成分を製造した。
比較例1のポリオール成分と比較して、使用するポリエーテルアルコール1および水の量を以下のように変更した:
54.0質量部のポリエーテルアルコール1、および
2.5質量部の水。
比較例1のポリオール成分と比較して、使用するポリエーテルアルコール1およびトリス−2−クロロイソプロピルホスファートの量を以下のように変更した:
60.65質量部のポリエーテルアルコール1、および
10質量部のトリス−2−クロロイソプロピルホスファート。
比較例1のポリオール成分中で使用するポリエーテルアルコール1およびポリエーテルアルコール2の量を以下のように変更した:
60.65質量部のポリエーテルアルコール1、および
0質量部のポリエーテルアルコール2。
56.15質量部のポリエーテルアルコール1、
6質量部のポリエーテルアルコール2、
プロピレンオキシドおよび開始剤としてグリセロールをベースとする、400mgKOH/gのヒドロキシル価を有する、20質量部のポリエーテルアルコール3、
15質量部のトリス−2−クロロイソプロピルホスファート、
1.8質量部のシリコーン泡安定剤(Goldschmidt製Tegostab(登録商標)B8443)、
0.2質量部の酢酸カリウムの50質量%エチレングリコール溶液、および
0.85質量部の水
から出発して混合することによって、ポリオール成分を製造した。
比較例5のポリオール成分と比較して、使用するポリエーテルアルコール1および水の量を以下のように変更した:
54.5質量部のポリエーテルアルコール1、および
2.5質量部の水。
比較例5のポリオール成分と比較して、使用する原料ポリエーテルアルコール1およびトリス−2−クロロイソプロピルホスファートの量を以下のように変更した:
61.15質量部のポリエーテルアルコール1、および
10質量部のトリス−2−クロロイソプロピルホスファート。
比較例1のポリオール成分と比較して、使用するポリエーテルアルコール1およびポリエーテルアルコール2の量を以下のように変更した:
60.65質量部のポリエーテルアルコール1、および
0質量部のポリエーテルアルコール2。
6質量部のポリエーテルアルコール2、
15質量部のトリス−2−クロロイソプロピルホスファート、
2.0質量部のシリコーン泡安定剤(Goldschmidt製Tegostab(登録商標)B8443)、
0.5質量部の、酢酸カリウムの50質量%エチレングリコール溶液、および
0.85質量部の水
から出発して混合することによって、ポリオール成分を製造した。
74.0質量部のポリエーテルエステルポリオール1、および
2.5質量部の水。
80.65質量部のポリエーテルエステルポリオール1、および
10質量部のトリス−2−クロロイソプロピルホスファート。
81.65質量部のポリエーテルエステルポリオール1、および
0質量部のポリエーテルアルコール2。
6質量部のポリエーテルアルコール2、
15質量部のトリス−2−クロロイソプロピルホスファート、
2.0質量部のシリコーン泡安定剤(Goldschmidt製Tegostab(登録商標)B8443)、
0.5質量部の、酢酸カリウムの50質量%エチレングリコール溶液、および
0.85質量部の水
から出発して混合することによって、ポリオール成分を製造した。
74.0質量部のポリエーテルエステルポリオール2、および
2.5質量部の水。
80.65質量部のポリエーテルエステルポリオール2、および
10質量部のトリス−2−クロロイソプロピルホスファート。
81.65質量部のポリエーテルエステルポリオール2、および
0質量部のポリエーテルアルコール2。
硬化度を、ボルト試験を用いて決定した。このために、成分をポリスチレンビーカー中で混合後、2.5、3、4、5、6、および7分において、半径10mmの球形キャップを備えた鋼ボルトを引張/圧縮試験機によって、形成されたキノコ形の泡中に10mmの深さで押し込んだ。ここで必要な最大の力(N単位)が、泡の硬化の測度である。3、4および5分後の最大の力の平均値を報告する。
ペンタン溶解度が測定される成分に、ペンタンを斬増的に添加することによって、ペンタン溶解度を決定した。ペンタンを、試験をする正確に100gの成分に、起こり得るペンタン溶解度に従って添加し、成分と混合した。混合物が濁ってもおらず、2つの相も持たない場合、さらなるペンタンを添加し、再度混合することになる。
グリセロール 5.0質量%、
オレイン酸 15.0質量%及び
PO 57.2質量%
からのポリエーテルエステルポリオール1
ヒドロキシル価:416mgKOH/g (DIN53240)
粘度(T=25℃):7210mPas (DIN53018)
グリセロール 19.9質量%、
オレイン酸メチル 13.5質量%及び
PO 58.07質量%
からのポリエーテルエステルポリオール2
ヒドロキシル価:464.5mgKOH/g (DIN53240)
粘度(T=25℃):783mPas (DIN53018)
表1および2の比較例に対する結果は、記載されている標準的な系は、混合の不均衡に関して極めて不安定であることを示す。組成のわずかな変化でさえ相分離を引き起こす(比較例2、3、4および8)。本発明の実施例1から8はすべて、ポリオール成分の組成の対応する変化に対して、安定な相の応答を有する。
Claims (12)
- A)有機もしくは修飾有機ポリイソシアナートまたはこれらの混合物と、
B)2個以上のイソシアナート反応性水素原子を有する化合物との、
C)場合により他のポリエステルポリオール、
D)場合によりポリエーテルオールポリオール、
E)場合により難燃剤、
F)1種または複数の発泡剤、
G)触媒、および
H)場合により他の助剤および/または添加剤
の存在下での、
反応によって得ることが可能な硬質ポリウレタンフォームであって、
成分B)は、
a1)15から40質量%の、2.5から8の平均官能基数を有する1種または複数のポリオールまたはポリアミンと、
a2)2から30質量%の、1種または複数の脂肪酸および/または脂肪酸モノエステルと、
a3)35から70質量%の、1種または複数の炭素原子2から4個のアルキレンオキシドと
の反応生成物を含む硬質ポリウレタンフォーム。 - 成分a1)のポリオールまたはポリアミンが、糖、ペンタエリトリトール、ソルビトール、トリメチロールプロパン、グリセロール、トリレンジアミン、エチレンジアミン、エチレングリコール、プロピレングリコールおよび水からなる群から選択される、請求項1に記載の硬質ポリウレタンフォーム。
- 前記成分a1)が、グリセロールとスクロースの混合物を含む、請求項2に記載の硬質ポリウレタンフォーム。
- 前記成分a2)が、オレイン酸またはオレイン酸誘導体を含む、請求項2または3に記載の硬質ポリウレタンフォーム。
- 成分a3)のアルキレンオキシドが、プロピレンオキシドである、請求項1から4のいずれか一項に記載の硬質ポリウレタンフォーム。
- 前記成分B)が、200から700mgKOH/gのOH価を有する、請求項1から5のいずれか一項に記載の硬質ポリウレタンフォーム。
- 前記成分B)が、2.5から8の官能基数を有する、請求項1から6のいずれか一項に記載の硬質ポリウレタンフォーム。
- 前記成分D)がプロポキシル化エチレンジアミンである、請求項1から7のいずれか一項に記載の硬質ポリウレタンフォーム。
- 前記成分D)が、グリセロールとスクロースの混合物をベースとするプロポキシル化ポリオールである、請求項1から7のいずれか一項に記載の硬質ポリウレタンフォーム。
- A)有機もしくは修飾有機ポリイソシアナートまたはこれらの混合物と、
B)1種または複数のポリエーテルエステルポリオールと、
C)場合により他のポリエステルポリオールと、
D)場合によりポリエーテルオールポリオールと、
E)場合により難燃剤と、
F)1種または複数の発泡剤と、
G)触媒と、
H)場合により他の助剤および/または添加剤と
の反応によって硬質ポリウレタンフォームを製造する方法であって、
成分B)は、
a1)15から40質量%の、2.5から8の平均官能基数を有する1種または複数のポリオールまたはポリアミンと、
a2)2から30質量%の、1種または複数の脂肪酸および/または脂肪酸モノエステルと、
a3)35から70質量%の、1種または複数の炭素原子2から4個のアルキレンオキシドと
の反応生成物を含む方法。 - 成分として
B)1種または複数のポリエーテルエステルポリオール、
C)場合により、請求項1に記載の他のポリエステルポリオール、
D)場合によりポリエーテルオールポリオール、
E)場合により難燃剤、
F)1種または複数の発泡剤、
G)触媒、および
H)場合により他の助剤および/または添加剤
を含むポリオール混合物。 - 25から90質量%のポリエーテルエステルポリオールB)、
0から20質量%の他のポリエステルポリオールC)、
0から35質量%のポリエーテルポリオールD)、
0から30質量%の難燃剤E)、および
1から40質量%の発泡剤F)、
0.001から5質量%の触媒G)、
0.01から10質量%の他の助剤および/または添加剤H)
を含む、請求項11に記載のポリオール混合物。
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CA3096666A1 (en) | 2018-04-10 | 2019-10-17 | Stepan Company | Polyol blends and rigid foams with improved low-temperature r-values |
PT3837296T (pt) * | 2018-08-16 | 2022-10-31 | Basf Se | Sistemas de espuma de pulverização de poliuretano respeitadores do ambiente |
KR20230029846A (ko) | 2020-06-25 | 2023-03-03 | 바스프 에스이 | 높은 압축 강도, 낮은 열 전도도, 및 높은 표면 품질을 갖는 폴리이소시아누레이트 수지 발포체 |
WO2023001687A1 (de) * | 2021-07-21 | 2023-01-26 | Basf Se | Polyurethanhartschaumstoffe auf basis von fettsäuremodifizierten polyetherpolyolen und vernetzenden polyesterpolyolen |
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EP2634201A1 (de) | 2013-09-04 |
CA2865311A1 (en) | 2013-09-06 |
WO2013127959A1 (de) | 2013-09-06 |
RU2014139357A (ru) | 2016-04-20 |
KR20140136960A (ko) | 2014-12-01 |
TR201902960T4 (tr) | 2019-03-21 |
AU2013224936B2 (en) | 2016-07-07 |
PT2820059T (pt) | 2019-04-02 |
AU2013224936A1 (en) | 2014-09-04 |
MX2014010355A (es) | 2014-10-14 |
RU2632198C2 (ru) | 2017-10-03 |
LT2820059T (lt) | 2019-03-25 |
PL2820059T3 (pl) | 2019-07-31 |
HUE042156T2 (hu) | 2019-06-28 |
KR102058225B1 (ko) | 2019-12-20 |
JP6286368B2 (ja) | 2018-02-28 |
EP2820059A1 (de) | 2015-01-07 |
CN104144961B (zh) | 2019-01-22 |
ES2717880T3 (es) | 2019-06-26 |
DK2820059T3 (en) | 2019-04-15 |
CN104144961A (zh) | 2014-11-12 |
EP2820059B1 (de) | 2018-12-26 |
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