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JP7573109B2 - Phenolic foam and method for producing same - Google Patents
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JP7573109B2 - Phenolic foam and method for producing same - Google Patents

Phenolic foam and method for producing same Download PDF

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JP7573109B2
JP7573109B2 JP2023526006A JP2023526006A JP7573109B2 JP 7573109 B2 JP7573109 B2 JP 7573109B2 JP 2023526006 A JP2023526006 A JP 2023526006A JP 2023526006 A JP2023526006 A JP 2023526006A JP 7573109 B2 JP7573109 B2 JP 7573109B2
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foam
closed cell
surface layer
layer portion
thickness
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キム,チェフン
ベ,ソンジェ
カン,ギルホ
キム,セビョル
パク,インソン
キム,ドフン
ハ,ヒェミン
パク,ゴンピョ
キム,ミョンフィ
キム,ハンス
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LX Hausys Ltd
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2361/00Characterised by the use of condensation polymers of aldehydes or ketones; Derivatives of such polymers
    • C08J2361/04Condensation polymers of aldehydes or ketones with phenols only

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  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
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Description

本発明は、フェノール発泡体及びこの製造方法に関する。 The present invention relates to a phenolic foam and a method for producing the same.

断熱材は、建築物におけるエネルギー損失を防ぐために必ず使用される物品である。地球温暖化により世界にグリーン成長の重要性が強調されていることから、エネルギー損失を最小化するため断熱性はさらに重要とされている。 Insulation is an essential item used in buildings to prevent energy loss. With global warming emphasizing the importance of green growth in the world, insulation is becoming even more important to minimize energy loss.

通常、断熱材の厚さを厚くすると、断熱性の確保は容易であるものの、断熱材の厚さが一定以上を超えると、厚さ方向に位置に応じて物性が変化し、発泡体が損傷しやすく、撓むなど、見掛け及び物性が低下し、熱伝導率まで低下する問題が発生する。 Usually, it is easy to ensure thermal insulation by increasing the thickness of the insulation material, but once the thickness of the insulation material exceeds a certain level, the physical properties change depending on the position in the thickness direction, and the foam becomes easily damaged and warped, resulting in a deterioration in appearance and physical properties, and even a decrease in thermal conductivity.

これによって、従来には高厚みの製品の物性を確保するために、発泡体全体において均一な物性を示し、発泡体の厚さ方向の中間部分(中心)を基準に対称的な物性を有する発泡体を製造しようとする傾向があった。 As a result, in the past, in order to ensure the physical properties of thick products, there was a tendency to manufacture foams that exhibit uniform physical properties throughout the foam and have symmetrical physical properties based on the middle part (center) of the foam in the thickness direction.

しかし、現実的に、厚さ全体にわたって物性の偏差を減らしながら対称構造を成すことは容易でなく、コスト及び生産効率面で非経済的であるという問題がある。 However, in reality, it is not easy to achieve a symmetrical structure while reducing the deviation in physical properties throughout the thickness, and this is uneconomical in terms of cost and production efficiency.

本発明の目的は、高厚みの発泡体の独立気泡率の分布を調節して生産効率を高め、より経済的に優れた物性を示す高厚みのフェノール発泡体を提供することである。また、本発明の目的は、発泡体の設置過程で発泡体が損傷することを防止して、発泡体の製造に際してだけでなく、長期間の使用過程でも、優れた断熱性及び圧縮強度などの物性を一定以上に維持し、撓みの発生を防止することができるフェノール発泡体を提供することである。 The object of the present invention is to provide a thick phenolic foam that exhibits excellent physical properties more economically by adjusting the distribution of the closed cell ratio of the thick foam to increase production efficiency. Another object of the present invention is to provide a phenolic foam that prevents the foam from being damaged during the installation process, and that maintains excellent physical properties such as insulation and compressive strength at a constant level not only during the production of the foam but also during long-term use, and prevents the occurrence of deflection.

また、本発明の目的は、前記フェノール発泡体を製造する方法を提供することである。 Another object of the present invention is to provide a method for producing the phenolic foam.

本発明の目的は、以上で言及した目的に制限されず、言及していない本発明の他の目的及び長所は、下記の説明によって理解することができ、本発明の実施例によってより明らかに理解することができる。また、本発明の目的及び長所は、特許請求の範囲に示した手段及びその組み合わせによって実現できることが分かりやい。 The object of the present invention is not limited to the object mentioned above, and other objects and advantages of the present invention not mentioned can be understood from the following description and can be more clearly understood from the examples of the present invention. It is also easy to understand that the object and advantages of the present invention can be realized by the means and combinations thereof shown in the claims.

本発明による厚さが90mm以上であるフェノール発泡体であって、前記発泡体のいずれか表面から、その表面に沿って厚さ方向にN(N≧7の奇数)本の切片に均分したとき、第1表層部(N)の独立気泡率は、第2表層部(N)の独立気泡率よりも低く、前記N本の切片のうち最小独立気泡率を有する切片(Nmin)は、前記第1表層部(N)と中間切片(N)との間に位置するフェノール発泡体を提供することができる。 The present invention provides a phenolic foam having a thickness of 90 mm or more, wherein when the foam is evenly divided into N slices (N≧7, where N is an odd number) from any surface of the foam in the thickness direction along the surface, the closed cell rate of a first surface layer portion (N 1 ) is lower than the closed cell rate of a second surface layer portion (N N ), and a slice (N min ) having the smallest closed cell rate among the N slices is located between the first surface layer portion (N 1 ) and an intermediate slice (N c ).

また、本発明によるフェノール系樹脂、発泡剤及び硬化剤を含む発泡組成物を、ノズルを用いて面材上に吐出するステップと、前記吐出した発泡組成物を発泡及び硬化するステップとを含み、前記ノズルは、長さ(L)/幅(W)が1以上2以下である形状の吐出口を有するフェノール発泡体の製造方法を提供することができる。 The present invention also provides a method for producing a phenolic foam, which includes the steps of discharging a foaming composition containing a phenolic resin, a foaming agent, and a curing agent onto a facing material using a nozzle, and foaming and curing the discharged foaming composition, the nozzle having a discharge outlet with a length (L)/width (W) ratio of 1 or more and 2 or less.

本発明によるフェノール発泡体は、高厚みの発泡体であって、より経済的に発泡体の設置過程における損傷を防止して、発泡体の製造に際してだけでなく、長期間の使用過程でも優れた断熱性及び圧縮強度などの物性を一定以上に表し、撓みの発生を防止することができる。 The phenolic foam of the present invention is a thick foam that is more economical in preventing damage during the foam installation process, and exhibits excellent physical properties such as excellent insulation and compressive strength to a certain level not only during foam production but also during long-term use, and can prevent the occurrence of deflection.

また、本発明によるフェノール発泡体の製造方法は、生産効率を高めて、より経済的に前記物性を有するフェノール発泡体を提供することができる。 The method for producing a phenolic foam according to the present invention can also improve production efficiency and provide a phenolic foam having the above physical properties more economically.

上述した効果並びに本発明の具体的な効果は、以下の発明を実施するための形態を説明するとともに記述する。 The above-mentioned effects and specific effects of the present invention will be described in the following description of the embodiment of the invention.

本発明の一具現例によるフェノール発泡体を厚さ方向にN本(N=9)均一に切断したことを示した模式図である。1 is a schematic diagram showing a phenolic foam according to an embodiment of the present invention being uniformly cut into N pieces (N=9) in the thickness direction. FIG. 本発明の一具現例による発泡組成物を吐出するノズルの吐出口を模式化した図面である。1 is a schematic view of a nozzle outlet for discharging a foam composition according to an embodiment of the present invention. 本発明の他の具現例によるコンベヤー上の下部面材に複数の吐出口を配置したことを簡略に示した模式図である。FIG. 13 is a schematic diagram showing a plurality of outlets arranged on a lower surface of a conveyor according to another embodiment of the present invention. 本発明のさらに他の具現例によるフェノール発泡体の撓み程度を測定する方法を簡略に示した模式図である。FIG. 4 is a schematic diagram illustrating a method for measuring the degree of deflection of a phenolic foam according to another embodiment of the present invention. 本発明のさらに他の具現例によるフェノール発泡体の寸法安定性を測定する方法を簡略に示した模式図である。FIG. 2 is a schematic diagram illustrating a method for measuring the dimensional stability of a phenolic foam according to another embodiment of the present invention.

前述した目的、特徴及び長所は、添付の図面を参照して詳細に後述され、これによって、本発明の属する技術分野における通常の知識を有する者は、本発明の技術的思想を容易に実施することができる。本発明を説明するにあたり、本発明に係る公知の技術に関する具体的な説明が本発明の要旨を曖昧にすると判断される場合には、詳細な説明を省略する。以下では、添付の図面を参照して、本発明による好ましい実施例を詳説することとする。図面における同じ参照符号は、同一又は類似の構成要素を示すために使われる。 The above-mentioned objects, features and advantages will be described in detail below with reference to the accompanying drawings, so that a person having ordinary skill in the art to which the present invention pertains can easily implement the technical idea of the present invention. In describing the present invention, if a detailed description of known technologies relating to the present invention is deemed to obscure the gist of the present invention, the detailed description will be omitted. Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings. The same reference symbols in the drawings are used to indicate the same or similar components.

以下では、本発明の幾つかの具現例によるフェノール発泡体を説明することとする。 Below, we will describe phenolic foams according to some embodiments of the present invention.

本発明の一具現例は、厚さが90mm以上であるフェノール発泡体であって、前記発泡体のいずれか表面から、その表面に沿って厚さ方向にN(N≧7の奇数)本の切片に均分したとき、第1表層部(N)の独立気泡率が第2表層部(N)の独立気泡率よりも低く、前記N本の切片のうち最小独立気泡率を有する切片(Nmin)が、前記第1表層部(N)と中間切片(N)との間に位置するフェノール発泡体を提供する。 One embodiment of the present invention provides a phenolic foam having a thickness of 90 mm or more, wherein when the foam is evenly divided into N slices (N≧7, where N is an odd number) from any surface of the foam in the thickness direction along the surface, the closed cell rate of a first surface layer portion (N 1 ) is lower than the closed cell rate of a second surface layer portion (N N ), and the slice (N min ) having the smallest closed cell rate among the N slices is located between the first surface layer portion (N 1 ) and an intermediate slice (N c ).

通常、発泡体は、厚さが厚いほど、断熱性の確保が容易である。しかし、発泡体の厚さが一定以上を超えると、発泡体の厚さ方向中心部の硬化反応によって内部発熱が大きくなるうえに、外部に熱が放散されにくく、発泡組成物の内部温度が過度に上昇する。これによって、発泡体の中心近くの気泡が破裂するなど、発泡体の厚さ方向に位置に応じて物性が顕著に変化し得、発泡体が損傷しやすく、撓みが発生し得る。発泡体に撓みが発生すると、見掛けの不良及び施工の不良が発生する可能性が大きく、長期間にわたり製品が収縮するなどの問題が発生する。そして、厚さが厚くなったにもかかわらず、熱伝導率は、却って低下し得る。これによって、従来には高厚みの製品の物性の確保と、撓みの防止のため、発泡体全体の物性を均一にし、発泡体の厚さ方向に中間部分を基準に物性が対称を成す発泡体を製造しようとする傾向があった。しかし、現実的に高厚みの発泡体において、厚さ全体にわたって物性を均一にしつつ、対称構造を成すことは容易でなく、コスト及び生産効率面で非経済的であるという問題がある。 In general, the thicker the foam, the easier it is to ensure thermal insulation. However, when the foam exceeds a certain thickness, the curing reaction at the center of the foam in the thickness direction increases internal heat generation, and the heat is difficult to dissipate to the outside, causing the internal temperature of the foam composition to rise excessively. As a result, the physical properties of the foam may change significantly depending on the position in the thickness direction of the foam, such as bubbles near the center of the foam bursting, and the foam may be easily damaged and warped. When the foam warps, there is a high possibility of apparent defects and poor construction, and problems such as product shrinkage over a long period of time may occur. In addition, even if the thickness is increased, the thermal conductivity may decrease. For this reason, in the past, in order to ensure the physical properties of a thick product and prevent warping, there was a tendency to manufacture a foam whose physical properties are symmetrical with respect to the middle part in the thickness direction of the foam, by making the physical properties of the entire foam uniform. However, in reality, it is not easy to make a symmetrical structure while making the physical properties uniform throughout the thickness of a thick foam, and there is a problem that it is uneconomical in terms of cost and production efficiency.

また、発泡体は、製造の際には、上部表層部及び下部表層部の区分が可能であるものの、施工の際には、発泡体の上下を区分し難しい。これによって、上部表層部と下部表層部のうちどの部位に衝撃が加わったかによって、物性の弱い部位が受ける衝撃は、大きく相違し得る。特に、断熱材は、例えば、天井用又は床用の断熱材などは、設置過程で作業者によって任意に位置が設定され、踏まれ、セメントなどを注いでから一定時間に熟成する過程を経ることになる。よって、製造の際には優れた物性を示す発泡体であっても、設置過程で発泡体の物性が弱い部位は、大きく損傷して、発泡体の使用中に断熱性及び圧縮強度などの物性が顕著に低下し、撓みが発生し得、これによって、熱伝導率が低下し得る。 In addition, although it is possible to separate the upper and lower surface layers of a foam during manufacturing, it is difficult to separate the upper and lower parts of the foam during construction. As a result, the impact on the weaker parts of the foam may vary greatly depending on which part of the upper or lower surface layer receives the impact. In particular, insulation materials, such as insulation materials for ceilings or floors, are arbitrarily positioned by workers during the installation process, stepped on, and cement is poured in and then allowed to mature for a certain period of time. Therefore, even if a foam shows excellent physical properties during manufacturing, the weaker parts of the foam may be significantly damaged during installation, causing a significant decrease in physical properties such as insulation and compressive strength during use, and deflection may occur, which may result in a decrease in thermal conductivity.

前記フェノール発泡体は、約90mm以上の厚さを有するものであって、発泡体の厚さ方向に中間部分を基準に非対称構造を有し、かつ発泡体における最小独立気泡率を有する位置を調節して、発泡体全体において断熱性、圧縮強度など、優れた物性を示し、撓みを防止することができる。そして、設置過程でフェノール発泡体の両表面のいずれか面に衝撃が加わっても、発泡体における弱い部位が受ける衝撃を同一、類似に下げることができる。これによって、前記フェノール発泡体は、施工過程を経た後にも長期間優れた物性を示すことができる。前記フェノール発泡体は、約110mm以上、約150mm以上、約180mm以上~300mmの厚さを有することができる。 The phenolic foam has a thickness of about 90 mm or more, and has an asymmetric structure based on the middle part in the thickness direction of the foam, and by adjusting the position of the foam with the minimum closed cell ratio, the foam as a whole exhibits excellent physical properties such as thermal insulation and compressive strength, and is prevented from warping. Even if an impact is applied to either of the two surfaces of the phenolic foam during the installation process, the impact received by the weak parts of the foam can be reduced to the same or similar extent. As a result, the phenolic foam can exhibit excellent physical properties for a long period of time even after the construction process. The phenolic foam can have a thickness of about 110 mm or more, about 150 mm or more, or about 180 mm or more to 300 mm.

前記フェノール発泡体は、発泡体の表面から、その表面に沿って厚さ方向にN(N≧7の奇数)本の切片に均分したとき、第1表層部(N)の独立気泡率が第2表層部(N)の独立気泡率よりも低く、前記N本の切片のうち最小独立気泡率を有する切片(Nmin)が、前記第1表層部(N)と中間切片(N)との間に位置する。 When the phenolic foam is evenly divided into N slices (N is an odd number greater than or equal to 7) from the surface of the foam in the thickness direction along the surface, the closed cell rate of a first surface layer portion (N 1 ) is lower than the closed cell rate of a second surface layer portion (N N ), and the slice (N min ) having the smallest closed cell rate among the N slices is located between the first surface layer portion (N 1 ) and an intermediate slice (N c ).

本発明は、発泡体の厚さによる独立気泡率の分布を測定するために、発泡体の表面から、その表面に沿って厚さ方向にN(N≧7の奇数)本の切片に均等に切断する。このとき、厚さは、面材上の発泡組成物が成長する方向(Z方向)を意味し、前記厚さ方向と垂直な面が表面であって、発泡体製造の際に面材が付着する面を意味する。前記発泡体は、面材がある場合、面材を除去し、正確な独立気泡率を測定するために、面材が付着していた発泡体の両表面をそれぞれ5mmずつ切断する。 In the present invention, in order to measure the distribution of the closed cell ratio according to the thickness of a foam, the foam is cut evenly into N pieces (N is an odd number of 7 or more) along the surface in the thickness direction from the surface. In this case, the thickness means the direction (Z direction) in which the foaming composition on the facing material grows, and the surface perpendicular to the thickness direction is the surface, which means the surface to which the facing material is attached during the production of the foam. If the foam has a facing material, the facing material is removed, and in order to accurately measure the closed cell ratio, both surfaces of the foam where the facing material was attached are cut by 5 mm each.

その後、前記発泡体の表面から、その表面に沿って厚さ方向にN(N≧7の奇数)本の切片に均分する。そして、各切片の独立気泡率を測定する。Nは、偶数を含む常数でも構わないが、発泡体における厚さ方向中心部を基準に物性が対称を成すかをより明確に確認するために、Nは、奇数であるのが好ましい。各々の切片は、約10mm~約30mmの厚さを有することができる。 Then, from the surface of the foam, divide it into N (N is an odd number greater than or equal to 7) equal pieces in the thickness direction along the surface. Then, measure the closed cell ratio of each piece. N may be a constant number including an even number, but it is preferable for N to be an odd number in order to more clearly confirm whether the physical properties are symmetrical with respect to the center of the foam in the thickness direction. Each piece can have a thickness of about 10 mm to about 30 mm.

前記フェノール発泡体は、第1表面及び第2表面を含み、前記第1表層部は、第1表面を含み、第2表層部は、前記第2表面を含む切片を意味する。前記発泡体の両表面を含む両端の2本の切片のうち、独立気泡率が低い切片をN(第1表層部)、他の切片をN(第2表層部)と示し、Nから順にN、N、N、N、...及びNと個々の切片を示す。そして、前記切片のうち、真ん中に位置した切片は、中間切片(N)と示す。すなわち、中間切片(N)は、前記第1表層部(N)及び前記第2表層部(N)の厚さ方向の1/2地点に位置した切片を意味する。例えば、図1は、本発明の一具現例によるフェノール発泡体を厚さ方向に9本(N=9)均一に切断したことを示した模式図であって、前記発泡体の両表面を含む両端の2本の切片のうち、独立気泡率が低い切片は、N(第1表層部)、他の切片は、N(第2表層部)となり、中間切片(N)は、Nとなる。そして、最小独立気泡率を有する切片(Nmin)が4番目切片、つまりNに位置したものを示したことである。 The phenolic foam includes a first surface and a second surface, the first surface layer portion includes the first surface, and the second surface layer portion means a slice including the second surface. Of the two slices at both ends including both surfaces of the foam, the slice with a low closed cell ratio is indicated as N 1 (first surface layer portion), and the other slice is indicated as N N (second surface layer portion), and the slices are indicated in order from N 1 to N 2 , N 3 , N 4 , N 5 , ... and N N. Among the slices, the slice located in the middle is indicated as the middle slice (N c ). In other words, the middle slice (N c ) means a slice located at 1/2 point in the thickness direction of the first surface layer portion (N 1 ) and the second surface layer portion (N N ). For example, Fig. 1 is a schematic diagram showing nine (N = 9) uniformly cut pieces of a phenolic foam according to an embodiment of the present invention in the thickness direction, in which the piece with the lowest closed cell content among the two pieces at both ends including both surfaces of the foam is N1 (first surface layer), the other piece is N9 (second surface layer), and the middle piece ( Nc ) is N5 . Also, the piece with the minimum closed cell content ( Nmin ) is located at the fourth piece, i.e., N4 .

前記フェノール発泡体は、第1表層部(N)の独立気泡率が第2表層部(N)の独立気泡率よりも低くて、非対称構造を成し、このとき、前記N本の切片のうち最小独立気泡率を有する切片(Nmin)が、前記第1表層部(N)と中間切片(N)との間に位置する。これによって、前記第1表層部及び第2表層部のいずれか面に衝撃が加わっても、最小独立気泡率を有する切片(Nmin)が受ける衝撃を同一、類似に低くして、発泡体全体において優れた断熱性などの物性とともに撓みを防止することができる。 The phenolic foam has an asymmetric structure in which the closed cell rate of the first surface layer portion (N 1 ) is lower than that of the second surface layer portion (N N ), and the piece (N min ) having the smallest closed cell rate among the N pieces is located between the first surface layer portion (N 1 ) and the middle piece (N c ). As a result, even if an impact is applied to either the first surface layer portion or the second surface layer portion, the impact received by the piece (N min ) having the smallest closed cell rate is similarly reduced, and the foam as a whole can be prevented from bending while maintaining excellent physical properties such as thermal insulation.

通常、高厚みの発泡体の場合、物性が厚さ方向に対称する分布を有するようにして、発泡体全体の物性を向上させようとするが、コストがかかり過ぎ、生産効率が落ちるところ、非経済的である。そして、発泡体の厚さが厚くなるほど、物性が対称構造の分布を有するようにすることは、現実的に不可能に近い。 Usually, in the case of thick foams, attempts are made to improve the physical properties of the entire foam by making the physical properties have a symmetrical distribution in the thickness direction, but this is uneconomical as it is too costly and reduces production efficiency. Furthermore, the thicker the foam, the more practically impossible it becomes to make the physical properties have a symmetrical distribution.

このため、前記フェノール発泡体は、第1表層部(N)の独立気泡率が第2表層部(N)の独立気泡率よりも低くて、非対称構造を有するようにして、より経済的に発泡体を製造しながらも、最小独立気泡率を有する切片(Nmin)が、第2表層部(N)の独立気泡率よりも低い独立気泡率を有する前記第1表層部(N)と中間切片(N)との間に位置して、目的とする効果を達することができる。例えば、最小独立気泡率を有する切片(Nmin)が中間切片(N)と独立気泡率の高い第2表層部(N)との間に位置する発泡体において、第1表層部(N)に衝撃が加わる場合は、問題にならない。しかし、第2表層部(N)に衝撃が加わる場合、最小独立気泡率を有する切片(Nmin)方向に撓みが大きく表れ、発泡体が大きく損傷して、使用過程で物性が顕著に低下し得る。前記フェノール発泡体は、前記構造を有することで、発泡体の厚さ方向において、物性が完全に対称を成す発泡体と同一、類似の効果を奏することができるところ、経済的である。 Therefore, the phenolic foam has an asymmetric structure in which the closed cell rate of the first surface layer portion (N 1 ) is lower than that of the second surface layer portion (N N ), so that the foam can be produced more economically, and the piece (N min ) having the minimum closed cell rate is located between the first surface layer portion (N 1 ) and the middle piece (N c ) having a lower closed cell rate than that of the second surface layer portion (N N ), thereby achieving the desired effect. For example, in a foam in which the piece (N min ) having the minimum closed cell rate is located between the middle piece (N c ) and the second surface layer portion (N N ) having a higher closed cell rate, there is no problem if an impact is applied to the first surface layer portion (N 1 ). However, when an impact is applied to the second surface layer (N N ), a large deflection occurs in the direction of the section (N min ) having the minimum closed cell ratio, and the foam is significantly damaged, and the physical properties may be significantly reduced during use. The phenolic foam has the above structure, and thus can achieve the same or similar effects as a foam whose physical properties are completely symmetrical in the thickness direction of the foam, and is therefore economical.

前記第1表層部(N)の独立気泡率と、前記第2表層部(N)の独立気泡率との差(=|第2表層部(N)の独立気泡率-第1表層部(N)の独立気泡率|)は、約0.05%~約5%であってもよい。例えば、約0.1%~約5%又は約0.1%~約3%であってもよい。前記第1表層部(N)と前記第2表層部(N)との独立気泡率の差が、上記範囲未満である場合には、コストが上昇し、生産効率が落ちて非経済的であり、上記範囲を超える場合には、発泡体全体は、優れた物性を有するようにするのに限界がある。 The difference between the closed cell rate of the first surface layer portion (N 1 ) and the closed cell rate of the second surface layer portion (N N ) (=|closed cell rate of the second surface layer portion (N N )−closed cell rate of the first surface layer portion (N 1 )|) may be about 0.05% to about 5%. For example, it may be about 0.1% to about 5% or about 0.1% to about 3%. If the difference in the closed cell rate between the first surface layer portion (N 1 ) and the second surface layer portion (N N ) is less than the above range, the cost increases and the production efficiency decreases, making it uneconomical, whereas if it exceeds the above range, there is a limit to how well the foam as a whole can have excellent physical properties.

前記第1表層部(N)の独立気泡率と、前記第2表層部(N)の独立気泡率は、それぞれ約85%以上であってもよい。例えば、約85%~約100%であってもよい。前記第1表層部(N)及び前記第2表層部(N)は、上記範囲の独立気泡率を有することで、優れた初期熱伝導率とともに、発泡体と空気の置換を防止して、断熱性能の経時変化量を低くし、優れた断熱性を示すことができる。 The closed cell ratio of the first surface layer portion (N 1 ) and the closed cell ratio of the second surface layer portion (N N ) may each be about 85% or more. For example, it may be about 85% to about 100%. By having the closed cell ratios in the above ranges, the first surface layer portion (N 1 ) and the second surface layer portion (N N ) can exhibit excellent initial thermal conductivity, prevent replacement of the foam with air, reduce the amount of change in thermal insulation performance over time, and exhibit excellent thermal insulation properties.

前記フェノール発泡体は、前記第2表層部(N)が最大独立気泡率を有し、前記第2表層部(N)と前記最小独立気泡率を有する切片(Nmin)との独立気泡率の差(△C2=|第2表層部(N)の独立気泡率-切片(Nmin)の独立気泡率|)は、約1~約20%であってもよい。例えば、約1~約15%又は約1%~約7%であってもよい。このとき、前記最小独立気泡率を有する切片(Nmin)と前記第2表層部(N)との独立気泡率の差が上記範囲を超える場合、気泡中の発泡剤と空気との置換速度が上昇して、熱伝導率の経時変化量が大きくなるだけでなく、高温環境下での収縮応力に耐えられる機械的強度が損傷してしまい、寸法変化率が顕著に悪化し得る。これによって、発泡体は、撓み現象が容易かつ大きく現れる。そして、前記第1表層部(N)と前記最小独立気泡率を有する切片(Nmin)との独立気泡率の差(△C1=|第1表層部(N)の独立気泡率-切片(Nmin)の独立気泡率|)は、約0.1~約20%であってもよい。例えば、約0.1~約10%であってもよい。 The phenol foam may have a maximum closed cell ratio in the second surface layer portion (N N ), and a difference in closed cell ratio between the second surface layer portion (N N ) and the piece (N min ) having the minimum closed cell ratio (ΔC2=|closed cell ratio of second surface layer portion (N N )-closed cell ratio of piece (N min )|) may be about 1 to about 20%. For example, it may be about 1 to about 15% or about 1% to about 7%. In this case, if the difference in closed cell ratio between the piece (N min ) having the minimum closed cell ratio and the second surface layer portion (N N ) exceeds the above range, the replacement speed of the foaming agent in the bubbles with air increases, and not only the change in thermal conductivity over time increases, but also the mechanical strength that can withstand shrinkage stress in a high-temperature environment is damaged, and the dimensional change rate may be significantly deteriorated. As a result, the foam may easily and significantly warp. The difference in closed cell ratio between the first surface layer portion (N 1 ) and the segment (N min ) having the minimum closed cell ratio (ΔC1=|closed cell ratio of the first surface layer portion (N 1 )−closed cell ratio of the segment (N min )|) may be about 0.1 to about 20%. For example, it may be about 0.1 to about 10%.

前記最小独立気泡率を有する切片(Nmin)は、約70%以上の独立気泡率を有することができる。例えば、約70%~約89%であってもよい。前記フェノール発泡体は、前記切片(Nmin)の独立気泡率を上記範囲に調節して、長期間にわたり低い熱伝導率を維持して、撓みの発生を防止し、寸法安定性を向上させることができる。例えば、上記範囲未満である場合、気泡内発泡剤と空気との置換速度が上昇して、熱伝導率の経時変化量が大きくなり得る。 The piece (N min ) having the minimum closed cell ratio may have a closed cell ratio of about 70% or more. For example, it may be about 70% to about 89%. By adjusting the closed cell ratio of the piece (N min ) in the above range, the phenolic foam can maintain low thermal conductivity for a long period of time, prevent warping, and improve dimensional stability. For example, if it is less than the above range, the replacement rate of the foaming agent in the cells with air increases, and the change in thermal conductivity over time may become large.

前記フェノール発泡体は、前記発泡体の全体厚に対するd1とd2の比率が約0.2:0.8~約0.45:0.55であってもよい。前記d1は、前記発泡体の全体厚に対する、前記第1表層部(N)から最小独立気泡率を有する切片(Nmin)までの厚さの比率(d1=第1表層部(N)の上部面から最小独立気泡率を有する切片(Nmin)の1/2地点までの厚さ/発泡体の全体厚)であり、前記d2は、前記発泡体の全体厚に対する、前記第2表層部(N)から最小独立気泡率を有する切片(Nmin)までの厚さの比率(d2=第2表層部(N)の下部面から最小独立気泡率を有する切片(Nmin)の1/2地点までの厚さ/発泡体の全体厚)であってもよい。このとき、前記発泡体の全体厚は、面材が付着していた発泡体の両表面をそれぞれ5mmずつ切断した後の発泡体の厚さを意味する。そして、前記d1及びd2は、図1に示すように、前記第1表層部の上部面又は前記第2表層部の下部面から最小独立気泡率を有する切片(Nmin)の厚さ方向の1/2地点までの垂直距離の比率を意味する。 The phenolic foam may have a ratio of d1 to d2 with respect to a total thickness of the foam of about 0.2:0.8 to about 0.45:0.55. The d1 may be a ratio of a thickness from the first surface portion (N 1 ) to a section (N min ) having a minimum closed cell content with respect to a total thickness of the foam (d1=thickness from an upper surface of the first surface portion (N 1 ) to a 1/2 point of the section (N min ) having a minimum closed cell content/total thickness of the foam), and the d2 may be a ratio of a thickness from the second surface portion (N N ) to a section (N min ) having a minimum closed cell content with respect to a total thickness of the foam (d2=thickness from a lower surface of the second surface portion (N 1 ) to a 1/2 point of the section (N min ) having a minimum closed cell content/total thickness of the foam). In this case, the total thickness of the foam means the thickness of the foam after cutting both surfaces of the foam to which the facing material was attached by 5 mm each, and d1 and d2 mean the ratio of the vertical distance from the upper surface of the first surface layer or the lower surface of the second surface layer to a 1/2 point in the thickness direction of the slice having the minimum closed cell ratio (N min ) as shown in FIG.

前記最小独立気泡率を有する切片(Nmin)は、前記第1表層部(N)と前記第2表層部(N)との関係において、前記地点に位置して、前記第1表層部及び第2表層部のいずれか面に衝撃が加わっても、最小独立気泡率を有する切片(Nmin)が受ける衝撃を同一、類似に低くして、発泡体全体において優れた断熱性などの物性とともに撓みを防止することができる。例えば、前記最小独立気泡率を有する切片(Nmin)が上記範囲を外れて、第1表層部(N)にさらに近く位置する場合、第1表層部(N)側の物性が顕著に低下して、発泡体全体の物性を一定以上に均一にすることが難しく、面材を含む第1表層部(N)の収縮が見掛けに表れ、第1表層部(N)方向に製品の撓みが大きく発生して、圧縮強度が低下するなどの問題があり得る。そして、最小独立気泡率を有する切片(Nmin)は、第2表層部(N)にさらに近く位置する場合、第2表層部(N)に衝撃が加わったとき、最小独立気泡率を有する切片(Nmin)が受ける衝撃の程度が急速に増加して、損傷しやすく、第2表層部(N)方向に製品が大きく撓むなどの問題があり得る。 The piece (N min ) having the minimum closed cell content is located at the point in relation to the first surface layer portion (N 1 ) and the second surface layer portion (N N ), and even if an impact is applied to either the first surface layer portion or the second surface layer portion, the impact received by the piece (N min ) having the minimum closed cell content is reduced to the same or similar extent, and the foam as a whole can be prevented from bending while having excellent physical properties such as thermal insulation. For example, if the piece (N min ) having the minimum closed cell content is out of the above range and located closer to the first surface layer portion (N 1 ), the physical properties on the first surface layer portion (N 1 ) side are significantly reduced, making it difficult to make the physical properties of the entire foam uniform to a certain degree or more, and shrinkage of the first surface layer portion (N 1 ) including the facing material is apparently manifested, and the product is greatly bent in the direction of the first surface layer portion (N 1 ), resulting in problems such as a reduction in compressive strength. Furthermore, if the piece having the minimum closed cell ratio (N min ) is located closer to the second surface layer portion (N N ), when an impact is applied to the second surface layer portion (N N ), the impact received by the piece having the minimum closed cell ratio (N min ) increases rapidly, making the piece more susceptible to damage and causing problems such as a large deflection of the product in the direction of the second surface layer portion (N N ).

前記フェノール発泡体は、各々の表層部(N,N)と、最小独立気泡率を有する切片(Nmin)との間の独立気泡率の差(△C1,△C2)を各々の表層部と最小独立気泡率を有する切片までの距離の比率(d1,d2)で割った値(Y)が、(|(△C2/d2)-(△C1/d1)|)=約0.1~約9であってもよい。例えば、約0.1~約6.5又は約0.1~約5であってもよい。前記Y値が上記範囲を超えると、厚さ方向に特定の位置で受ける衝撃が大きくなるか、発泡体全体の物性が低下して、撓みが発生する問題があり得る。 The phenolic foam may have a value (Y) obtained by dividing the difference (ΔC1, ΔC2) in the closed cell ratio between each of the surface layers (N 1 , N N ) and the section (N min ) having the minimum closed cell ratio by the ratio (d1, d2) of the distance between each of the surface layers and the section having the minimum closed cell ratio, such that (|(ΔC2/d2)-(ΔC1/d1)|) is about 0.1 to about 9. For example, it may be about 0.1 to about 6.5 or about 0.1 to about 5. If the Y value exceeds the above range, there may be a problem that an impact received at a specific position in the thickness direction becomes large or the physical properties of the entire foam are deteriorated, causing deflection.

前記フェノール発泡体は、上記のような独立気泡率の分布を有することで、発泡体全体において、優れた物性を示すことができ、長期間の使用にもかかわらず、優れた熱伝導率を維持することができる。 The phenol foam has the above-mentioned distribution of closed cell ratio, which allows the foam to exhibit excellent physical properties throughout and maintain excellent thermal conductivity even after long-term use.

具体的に、前記フェノール発泡体は、KS M ISO 844による圧縮強度が約100kPa~約200kPaであってもよい。例えば、約115kPa~約200kPaであってもよい。圧縮強度は、発泡体が破断するときの圧力を意味する。前記フェノール発泡体は、上記範囲の圧縮強度を有することで、物性間に優れた均衡を維持し、流通及び施工後にも優れた長期耐久性を示すことができる。 Specifically, the phenolic foam may have a compressive strength according to KS M ISO 844 of about 100 kPa to about 200 kPa. For example, it may be about 115 kPa to about 200 kPa. Compressive strength refers to the pressure at which the foam breaks. By having a compressive strength in the above range, the phenolic foam can maintain an excellent balance between physical properties and exhibit excellent long-term durability even after distribution and construction.

前記フェノール発泡体は、約0%~約2.0%の寸法変化率を有することができる。例えば、前記フェノール発泡体は、約0%~約1.0%又は約0%~約0.7%の寸法変化率を有することができる。このとき、寸法変化率は、実験例4に記載の方法で測定することができる。 The phenol foam may have a dimensional change rate of about 0% to about 2.0%. For example, the phenol foam may have a dimensional change rate of about 0% to about 1.0% or about 0% to about 0.7%. In this case, the dimensional change rate can be measured by the method described in Experimental Example 4.

発泡体は、図4に示すように、25℃、相対湿度60%で、7日経過すると、発泡体の表面部が床面に向かって凹に撓む場合(I)、或いは発泡体の表面部が天井に向かって凸に撓む場合(II)が発生し得る。このとき、上記(I)の場合は、角部分(P1~P4)の変化が、そして、上記(II)の場合は、発泡体の長さ方向の2辺と床面との間の最大隔離距離(R1,R2)が、発泡体が外部衝撃に対して受ける損傷及び発泡体の全体変形に影響を及ぼし得る。前記フェノール発泡体は、上記(I)の場合、及び/又は上記(II)の場合において、それぞれ約0cm~約1.5cmの平均撓みを有することができる。または、それぞれ約0.1cm~約0.7cm又は約0.1cm~約0.5cmの平均撓みを有することができる。 As shown in FIG. 4, after 7 days at 25°C and 60% relative humidity, the foam may bend in a concave manner toward the floor (I) or in a convex manner toward the ceiling (II). In this case, the change in the corners (P1 to P4) in the case of (I) and the maximum separation distance (R1, R2) between the two longitudinal sides of the foam and the floor may affect the damage and overall deformation of the foam due to external impact. The phenol foam may have an average deflection of about 0 cm to about 1.5 cm in the case of (I) and/or (II), respectively. Alternatively, the phenol foam may have an average deflection of about 0.1 cm to about 0.7 cm or about 0.1 cm to about 0.5 cm, respectively.

前記フェノール発泡体は、KS L 9016による平均温度20℃で測定した熱伝導率が、約0.017W/m・K~約0.020W/m・Kであってもよい。 The phenolic foam may have a thermal conductivity of about 0.017 W/m·K to about 0.020 W/m·K measured at an average temperature of 20°C according to KS L 9016.

そして、前記フェノール発泡体は、EN13823に従って、70℃で、7日間乾燥した後に、110℃で、14日間乾燥した後、平均温度20℃で測定した熱伝導率が約0.018W/m・K~約0.022W/m・Kであってもよい。 The phenolic foam may have a thermal conductivity of about 0.018 W/m·K to about 0.022 W/m·K measured at an average temperature of 20°C after drying at 70°C for 7 days and then at 110°C for 14 days in accordance with EN13823.

前記フェノール発泡体は、独立気泡率を上記のような分布で含み、優れた圧縮強度などの物性を示し、撓みを防止して、長期熱伝導率においても約10%以下の経時変化を示すことができる。 The phenol foam contains the closed cell rate in the above-mentioned distribution, exhibits excellent physical properties such as compressive strength, prevents bending, and shows a change in thermal conductivity over time of about 10% or less.

本発明の他の具現例は、フェノール系樹脂、発泡剤及び硬化剤を含む発泡組成物を、ノズルを用いて面材上に吐出するステップと、前記吐出した発泡組成物を発泡及び硬化するステップとを含み、前記ノズルは、長さ(L)/幅(W)が1以上2以下である形状の吐出口を有するフェノール発泡体の製造方法を提供する。 Another embodiment of the present invention provides a method for producing a phenolic foam, comprising the steps of discharging a foaming composition containing a phenolic resin, a foaming agent, and a curing agent onto a facing material using a nozzle, and foaming and curing the discharged foaming composition, the nozzle having a discharge outlet with a length (L)/width (W) ratio of 1 to 2.

上記製造方法によって前述したように、特定した独立気泡率の分布を有し、発泡体全体において優れた物性を有するフェノール発泡体をより経済的に製造することができる。そして、上記製造方法に従って製造された前記フェノール発泡体は、前記第1表層部及び前記第2表層部のいずれか面に衝撃が加わっても、最小独立気泡率を有する切片(Nmin)が受ける衝撃を同一、類似に低くして、発泡体全体において優れた断熱性、圧縮強度などの物性とともに撓みを防止することができる。前記フェノール発泡体の厚さ、独立気泡率など、上述した事項は、下記で特に記載したことを除いては、前述のとおりである。 As described above, the above-mentioned manufacturing method can more economically manufacture a phenolic foam having a specific distribution of closed cell ratio and excellent physical properties throughout the foam. Furthermore, the phenolic foam manufactured according to the above-mentioned manufacturing method can reduce the impact received by the piece having the minimum closed cell ratio (N min ) to the same or similar extent even when an impact is applied to either the first surface layer portion or the second surface layer portion, thereby preventing deflection throughout the foam as well as providing excellent physical properties such as thermal insulation and compressive strength. The above-mentioned items such as the thickness and closed cell ratio of the phenolic foam are as described above, except as otherwise specified below.

通常の厚さを有するフェノール発泡体の場合、発泡組成物を第1面材上に、1つのノズルを用いて連続して吐出した後、硬化炉内コンベヤーの間で板状に成形すると、発泡組成物が設定された厚さまで迅速に発泡、硬化反応し、反応時に生成された反応熱は、表面の面材を介して容易に放射されて、厚さ全体にわたって均一な物性を有することが難しくない。一方、厚さ90mm以上のフェノール発泡体の場合、発泡体の厚さ方向中心部の硬化反応によって内部発熱が大きくなり、外部に熱が放散しにくく、発泡組成物の内部温度が過度に上昇する。これによって、発泡体の中心近くの気泡が破裂しやすい。また、第1面材(下部面材)上に吐出した発泡組成物は、第2面材(上部面材)方向(Z方向)に膨張することにおいて、製品の厚さが厚い場合、発泡-硬化に要する時間が相対的に長くなる。これによって、発泡組成物が第1面材(下部面材)に留まる時間が長くなり、第1面材(下部面材)に発泡組成物が次第に蓄積されて、相対的に過度な膨張が発生し、第1面材(下部面材)近くの気泡が破裂しやすい傾向を示し、発泡体の厚さが厚くなるほど、物性のバラツキが顕著に現れ、これによって、発泡体の全体物性が低下し得る。これを克服するために、上下部面材上に、各々のノズルを用いて個別に発泡組成物を吐出させる方法が提案されたりもするが、かかる方法は、複雑な装置が必要であり、コストが上昇する問題がある。 In the case of a phenolic foam having a normal thickness, when the foaming composition is continuously discharged onto the first face material using one nozzle and then molded into a plate between the conveyors in the curing oven, the foaming composition rapidly foams and cures to the set thickness, and the reaction heat generated during the reaction is easily radiated through the surface face material, so it is not difficult to have uniform physical properties throughout the thickness. On the other hand, in the case of a phenolic foam having a thickness of 90 mm or more, internal heat generation increases due to the curing reaction in the center of the foam in the thickness direction, and the heat is difficult to dissipate to the outside, so the internal temperature of the foaming composition rises excessively. As a result, the bubbles near the center of the foam are likely to burst. In addition, the foaming composition discharged onto the first face material (lower face material) expands in the direction of the second face material (upper face material) (Z direction), and when the product is thick, the time required for foaming and curing is relatively long. As a result, the foaming composition remains on the first face material (lower face material) for a longer period of time, and gradually accumulates on the first face material (lower face material), causing relatively excessive expansion, and the bubbles near the first face material (lower face material) tend to burst more easily. The thicker the foam, the more pronounced the variation in physical properties becomes, which can lead to a deterioration in the overall physical properties of the foam. To overcome this, a method has been proposed in which the foaming composition is discharged individually onto the upper and lower faces using nozzles, but this method requires complex equipment and increases costs.

本発明の他の具現例による前記フェノール発泡体の製造方法は、フェノール系樹脂、発泡剤及び硬化剤を含む発泡組成物を、ノズルを用いて面材3上に吐出するステップを含む。このとき、前記ノズルの入口である吐出口10は、長さ(L)/幅(W)が1以上2以下である形状を有することができる。例えば、図2に示したように、長さ(L)が幅(W)よりも長い楕円状を有することができ、前記長さ(L)/幅(W)が1超2以下であってもよい。前記吐出口は、組成物が吐出する入口を意味する。このとき、楕円において、長さ(L)は長軸、幅(W)は短軸の長さを意味する。図3に示したように、前記吐出口の長さ(L)方向は、発泡体の厚さ方向(Z方向)と平行であり、前記吐出口の幅(W)方向は、発泡体の幅方向(Y方向)と平行な方向に位置することができる。 The method for producing the phenolic foam according to another embodiment of the present invention includes a step of discharging a foaming composition including a phenolic resin, a foaming agent, and a curing agent onto a facing material 3 using a nozzle. At this time, the outlet 10, which is the inlet of the nozzle, may have a shape in which the length (L)/width (W) is 1 or more and 2 or less. For example, as shown in FIG. 2, it may have an elliptical shape in which the length (L) is longer than the width (W), and the length (L)/width (W) may be greater than 1 and less than 2. The outlet means an inlet through which the composition is discharged. In this case, in the ellipse, the length (L) means the length of the major axis, and the width (W) means the length of the minor axis. As shown in FIG. 3, the length (L) direction of the outlet may be parallel to the thickness direction (Z direction) of the foam, and the width (W) direction of the outlet may be parallel to the width direction (Y direction) of the foam.

前記ノズルの吐出口は、1以上2以下である長さ(L)/幅(W)(aspect ratio)を有することができる。例えば、前記ノズルの吐出口は、1超2以下である楕円状の吐出口を有することができる。これによって、硬化している気泡が発泡組成物の移動によって崩れることを防止し、発泡組成物が吐出される面材(例:下部面材)近くにおいて、発泡組成物が過度に発泡及び膨張するなどの問題を防止することができる。例えば、ノズルの吐出口が楕円ではない、長方形構造を有する場合、吐出口の角近くに硬化物が蓄積するなどの問題があり得る。そして、前記吐出口が円形又は楕円状を有するものの、長さ(L)/幅(W)が上記範囲未満である場合、発泡組成物が吐出する下部面材近くにおいて、過度な発泡及び膨張が発生して、気泡が容易に破泡するなどの問題があり得る。長さ(L)/幅(W)の比が上記範囲を超える場合、発泡組成物が発泡体の幅方向(Y方向、発泡組成物の吐出方向と直交する方向)に広がる量が増加しながら、加熱によって硬化している気泡が発泡組成物の移動によって崩れ、発泡体の厚さ方向(Z方向)への発泡及び膨張速度がさらに遅くなり、発泡組成物が下部面材近くに留まる時間及び量が多くなる問題と、気泡が破泡するなどの問題があり得る。 The nozzle outlet may have a length (L)/width (W) (aspect ratio) of 1 or more and 2 or less. For example, the nozzle outlet may have an elliptical outlet having a length (L)/width (W) ratio of more than 1 and 2 or less. This prevents the hardened bubbles from collapsing due to the movement of the foaming composition, and prevents problems such as excessive foaming and expansion of the foaming composition near the surface material (e.g., the lower surface material) from which the foaming composition is discharged. For example, if the nozzle outlet has a rectangular structure rather than an ellipse, there may be problems such as the hardened material accumulating near the corners of the outlet. And, if the outlet has a circular or elliptical shape but the length (L)/width (W) is less than the above range, there may be problems such as excessive foaming and expansion occurring near the lower surface material from which the foaming composition is discharged, causing bubbles to easily break. If the length (L)/width (W) ratio exceeds the above range, the amount of the foaming composition spreading in the width direction of the foam (Y direction, the direction perpendicular to the direction of extrusion of the foaming composition) increases, and the bubbles that have hardened due to heating collapse due to the movement of the foaming composition, further slowing the foaming and expansion speed in the thickness direction of the foam (Z direction), which can cause problems such as an increase in the time and amount of the foaming composition remaining near the lower surface material and bubbles breaking.

前記吐出口は、約10mm~約100mmの長さ(L)を有することができる。前記吐出口の長軸である長さ(L)が上記範囲未満である場合、ノズルの吐出時に発生する圧力が上昇し得、上記範囲を超える場合、圧力が低くなりながら適宜な発泡が行われない問題があり得る。 The outlet can have a length (L) of about 10 mm to about 100 mm. If the length (L), which is the major axis of the outlet, is less than the above range, the pressure generated when the nozzle is discharged may increase, and if it exceeds the above range, there may be a problem that the pressure is low and proper foaming is not performed.

前記発泡組成物は、約30kg/min~約100kg/minに吐出し得る。 The foamable composition can be discharged at about 30 kg/min to about 100 kg/min.

前記吐出時の前記発泡組成物の粘度は、25℃で、約5,000cps~約40,000cpsであってもよい。前記発泡組成物は、上記範囲の粘度を有することで、発泡及び硬化に適宜なスラーリ状に吐出することができる。 The viscosity of the foaming composition at the time of ejection may be about 5,000 cps to about 40,000 cps at 25°C. By having a viscosity in the above range, the foaming composition can be ejected in a slurry form suitable for foaming and curing.

前記吐出時の前記発泡組成物の温度は、約0℃~約40℃であってもよい。温度範囲が上記範囲未満である場合、吐出物の粘度が過度に上昇して、吐出し難しい問題があり、上記範囲を超える場合、発泡剤が容易に揮発して、熱伝導率が低下する問題があり得る。 The temperature of the foaming composition during the ejection may be about 0°C to about 40°C. If the temperature range is less than the above range, the viscosity of the ejected material increases excessively, making it difficult to eject, and if the temperature range is exceeded, the foaming agent easily volatilizes, decreasing the thermal conductivity.

前記フェノール発泡体の製造方法は、図3に示したように、発泡組成物の流れ方向(X軸、つまり面材3の走行方向)と直交する方向(Y軸方向、発泡体の幅方向)に沿って配置された前記吐出口10を有する複数のノズルを備えることができる。具体的に、前記ノズルは、約4本~約12本であってもよい。前記ノズルは、等間隔で並列に配置されていてもよい。 As shown in FIG. 3, the method for producing the phenolic foam may include a plurality of nozzles having the discharge ports 10 arranged along a direction (Y-axis direction, width direction of the foam) perpendicular to the flow direction of the foam composition (X-axis, i.e., the running direction of the facing material 3). Specifically, the number of the nozzles may be about 4 to about 12. The nozzles may be arranged in parallel at equal intervals.

前記製造方法は、前記吐出口10を有する前記本数のノズルを均一な間隔で並列配置して、発泡組成物が成長する方向(Z軸方向、発泡体の厚さ方向)にだけではなく、発泡組成物の流れ方向(X軸、つまり面材の走行方向)と直交する方向(Y軸方向、発泡体の幅方向)に均一な膨張を誘導することができる。このため、気泡の成長及び分布を適宜調節することができる。 The manufacturing method described above arranges the number of nozzles having the discharge outlets 10 in parallel at uniform intervals, and can induce uniform expansion not only in the direction in which the foaming composition grows (Z-axis direction, thickness direction of the foam), but also in the direction perpendicular to the flow direction of the foaming composition (X-axis, i.e., the running direction of the facing material) (Y-axis direction, width direction of the foam). This allows the growth and distribution of bubbles to be appropriately adjusted.

前記発泡組成物は、フェノール系樹脂、発泡剤及び硬化剤を含む。前記フェノール系樹脂は、フェノール及びホルムアルデヒドが反応して得ることができ、例えば、レゾール系フェノール樹脂(以下、「レゾール樹脂」)を含むことができる。前記フェノール系樹脂は、前記フェノール発泡体内に約30重量%~約90重量%、又は約50重量%~約90重量%、又は約55重量%~約90重量%の含量で含まれていてもよい。前記フェノール発泡体は、前記フェノール系樹脂を上記範囲内の含量で含むことで、小さい大きさの発泡セルを安定的に形成し、優れた熱伝導度を具現することができる。 The foaming composition includes a phenolic resin, a foaming agent, and a curing agent. The phenolic resin can be obtained by reacting phenol and formaldehyde, and can include, for example, a resol-type phenolic resin (hereinafter, "resole resin"). The phenolic resin may be included in the phenolic foam in an amount of about 30% to about 90% by weight, about 50% to about 90% by weight, or about 55% to about 90% by weight. By including the phenolic resin in an amount within the above range, the phenolic foam can stably form small foam cells and realize excellent thermal conductivity.

前記フェノール発泡体は、発泡剤を含むことができる。例えば、前記発泡剤は、ヒドロフルオロオレフィン(hydrofluoroolefin,HFO)系化合物、炭化水素系化合物、及びこれらの組み合わせからなる群から選択された1つを含むことができる。具体的に、前記ヒドロフルオロオレフィン系化合物は、例えば、モノクロロトリフルオロプロペン、トリフルオロプロペン、テトラフルオロプロペン、ペンタフルオロプロペン、ヘキサフルオロブテン、及びこれらの組み合わせからなる群から選択される少なくとも1つを含むことができる。そして、前記炭化水素系化合物は、炭素数1本~8本の炭化水素を含むことができる。例えば、前記炭化水素系化合物は、ジクロロエタン、プロピルクロライド、イソプロピルクロライド、ブチルクロライド、イソブチルクロライド、ペンチルクロライド、イソペンチルクロライド、n-ブタン、イソブタン、n-ペンタン、イソペンタン、シクロペンタン、ヘキサン、ヘプタン、シクロペンタン、及びこれらの組み合わせからなる群から選択される少なくとも1つを含むことができる。または、前記炭化水素系化合物は、炭素数1本~5本の炭化水素であって、ジクロロエタン、プロピルクロライド、イソプロピルクロライド、ブチルクロライド、イソブチルクロライド、ペンチルクロライド、イソペンチルクロライド、n-ブタン、イソブタン、n-ペンタン、イソペンタン、シクロペンタン、及びこれらの組み合わせからなる群から選択される少なくとも1つを含み、環境にやさしいと共に、優れた断熱性を示すことができる。前記発泡剤は、前記フェノール発泡体を約100重量部を基準に約6重量部~約13重量部となるように含まれていてもよい。 The phenol foam may include a foaming agent. For example, the foaming agent may include one selected from the group consisting of hydrofluoroolefin (HFO)-based compounds, hydrocarbon-based compounds, and combinations thereof. Specifically, the hydrofluoroolefin-based compounds may include at least one selected from the group consisting of monochlorotrifluoropropene, trifluoropropene, tetrafluoropropene, pentafluoropropene, hexafluorobutene, and combinations thereof. The hydrocarbon-based compounds may include hydrocarbons having 1 to 8 carbon atoms. For example, the hydrocarbon-based compounds may include at least one selected from the group consisting of dichloroethane, propyl chloride, isopropyl chloride, butyl chloride, isobutyl chloride, pentyl chloride, isopentyl chloride, n-butane, isobutane, n-pentane, isopentane, cyclopentane, hexane, heptane, cyclopentane, and combinations thereof. Alternatively, the hydrocarbon compound is a hydrocarbon having 1 to 5 carbon atoms, and includes at least one selected from the group consisting of dichloroethane, propyl chloride, isopropyl chloride, butyl chloride, isobutyl chloride, pentyl chloride, isopentyl chloride, n-butane, isobutane, n-pentane, isopentane, cyclopentane, and combinations thereof, and is environmentally friendly and exhibits excellent heat insulation. The foaming agent may be included in an amount of about 6 to about 13 parts by weight based on about 100 parts by weight of the phenol foam.

前記フェノール発泡体は、硬化剤を含む。前記硬化剤は、酸性硬化剤であって、トルエンスルホン酸、キシレンスルホン酸、ベンゼンスルホン酸、フェノールスルホン酸、エチルベンゼンスルホン酸、スチレンスルホン酸、ナフタレンスルホン酸、及びこれらの組み合わせからなる群から選択された1つの酸性硬化剤を含むことができる。 The phenolic foam includes a hardener. The hardener may include an acidic hardener selected from the group consisting of toluenesulfonic acid, xylenesulfonic acid, benzenesulfonic acid, phenolsulfonic acid, ethylbenzenesulfonic acid, styrenesulfonic acid, naphthalenesulfonic acid, and combinations thereof.

前記酸性硬化剤は、前記フェノール発泡体100重量部に対し、約9重量部~約20重量部の含量で含まれていてもよい。前記フェノール発泡体は、前記硬化剤を上記範囲の含量で含み、適正の架橋、硬化及び発泡性を示すことができる。 The acidic hardener may be present in an amount of about 9 parts by weight to about 20 parts by weight per 100 parts by weight of the phenolic foam. The phenolic foam may exhibit appropriate crosslinking, hardening and foaming properties by containing the hardener in the above range.

前記フェノール発泡体の製造方法は、前記吐出した発泡組成物を発泡及び硬化するステップを含む。前記フェノール発泡体は、硬化炉内コンベヤーの間で板状に発泡及び硬化することができる。例えば、約40℃~約90℃の温度条件下で発泡及び硬化し得る。また、前記発泡及び硬化は、約2分~約20分の間に行うことができるものの、これに制限されず、発明の目的及び用途によって適宜に異なり得る。 The method for producing the phenolic foam includes a step of foaming and curing the discharged foam composition. The phenolic foam can be foamed and cured into a plate shape between conveyors in a curing oven. For example, the foaming and curing can be performed under temperature conditions of about 40°C to about 90°C. The foaming and curing can be performed for about 2 minutes to about 20 minutes, but is not limited thereto and can vary depending on the purpose and use of the invention.

本発明のさらに他の具現例は、前記フェノール発泡体を含む断熱材を提供する。前記フェノール発泡体は、優れた圧縮強度、撓みの防止及び優れた断熱性を同時に満たせ、建築用断熱材の用途に使用することができる。 Yet another embodiment of the present invention provides an insulating material containing the phenolic foam. The phenolic foam simultaneously exhibits excellent compressive strength, resistance to deflection, and excellent insulating properties, and can be used as an insulating material for buildings.

前記建築用断熱材は、例えば、前記フェノール発泡体の一面又は両面上に面材をさらに含むことができ、前記面材としてアルミニウムを含み、難燃性をさらに向上させることができる。 The building insulation material can further include a facing material on one or both sides of the phenolic foam, and the facing material can include aluminum to further improve flame retardancy.

(実施例)
実施例1:
レゾール樹脂100重量部に対して、硬化剤としてトルエンスルホン酸18重量部、発泡剤としてシクロペンタン10重量部、および界面活性剤を含む発泡組成物(25℃、20,000cps)を準備した。
(Example)
Example 1:
A foaming composition (25° C., 20,000 cps) containing 100 parts by weight of resol resin, 18 parts by weight of toluenesulfonic acid as a curing agent, 10 parts by weight of cyclopentane as a foaming agent, and a surfactant was prepared.

長さ(L)/幅(W)が1.5である楕円吐出口(長さ(L)=10mm)を有するノズルを、コンベヤー7の移動方向(X軸、つまり面材の走行方向)と直交する方向(Y軸方向、発泡体の幅方向)に沿って下部面材上に等間隔で6本を並列配置した。 Six nozzles with elliptical outlets (length (L) = 10 mm) with a length (L) / width (W) ratio of 1.5 were arranged in parallel at equal intervals on the lower surface material along a direction (Y-axis direction, width direction of the foam) perpendicular to the movement direction of the conveyor 7 (X-axis, i.e., the running direction of the surface material).

そして、10m/minの速度で移動し、幅1200mm及び厚さ190mmの大きさを有し、70℃雰囲気温度であるコンベヤー上に、前記個々の吐出口を用いて前記発泡組成物を40k/min吐出し、発泡及び硬化して、厚さ190mmのフェノール発泡体を製造した。 The foaming composition was then discharged at 40 kg/min using the individual discharge ports onto a conveyor moving at a speed of 10 m/min, measuring 1200 mm wide and 190 mm thick, and having an ambient temperature of 70°C, where it was foamed and cured to produce a phenolic foam with a thickness of 190 mm.

実施例2:
長さ(L)/幅(W)が1である円形吐出口(長さ(L)=10mm)を有するノズルを用いたことを除いては、実施例1と同様の方法でフェノール発泡体を製造した。
Example 2:
A phenolic foam was produced in the same manner as in Example 1, except that a nozzle having a circular outlet (length (L) = 10 mm) with a length (L) / width (W) ratio of 1 was used.

比較例1:
長さ(L)/幅(W)が2.5である楕円吐出口(長さ(L)=10mm)を有するノズルを用いたことを除いては、実施例1と同様の方法でフェノール発泡体を製造した。
Comparative Example 1:
A phenolic foam was produced in the same manner as in Example 1, except that a nozzle having an elliptical outlet (length (L) = 10 mm) with a length (L) / width (W) ratio of 2.5 was used.

比較例2:
長さ(L)/幅(W)が0.5である楕円吐出口(長さ(L)=10mm)を有するノズルを用いたことを除いては、実施例1と同様の方法でフェノール発泡体を製造した。
Comparative Example 2:
A phenol foam was produced in the same manner as in Example 1, except that a nozzle having an elliptical outlet (length (L) = 10 mm) with a length (L) / width (W) ratio of 0.5 was used.

評価
実験例1:各切片の独立気泡率
実施例及び比較例のフェノール発泡体に付着した面材を除去し、面材が付着していた発泡体の両表面をそれぞれ5mmずつ切断した。
Evaluation Experimental Example 1: Closed cell ratio of each cut piece The face material attached to the phenol foam of each of the examples and comparative examples was removed, and both surfaces of the foam to which the face material had been attached were cut by 5 mm each.

その後、前記発泡体の表面から、その表面に沿って厚さ方向に9本(N=9)の切片に均一に切断し、切断前の発泡体の厚さ方向全体にわたって中間部分を含むように、2.5cm(L)×2.5cm(W)×2.0cm(T)の大きさの発泡体切片を製造した。このとき、前記発泡体の両表面を含む両端の2本の切片のうち、独立気泡率が低い切片をN(第1表層部)、他の切片をN(第2表層部)と示し、Nから順にN、N、N、N、N、N、N、及びNと個々の切片を示した。これによって、中間切片(N)は、Nとなる。 Then, the foam was cut uniformly into nine pieces (N=9) from the surface in the thickness direction along the surface, and foam pieces of 2.5 cm (L) x 2.5 cm (W) x 2.0 cm (T) were produced so as to include the middle part throughout the entire thickness direction of the foam before cutting. At this time, of the two pieces at both ends including both surfaces of the foam, the piece with the lower closed cell ratio was designated N1 (first surface layer part), and the other piece was designated N9 (second surface layer part), and the individual pieces were designated N2 , N3 , N4 , N5 , N6 , N7 , N8 , and N9 in order from N1 . As a result, the middle piece ( Nc ) became N5 .

そして、前記個々の試片(N~N)に対して、KS M ISO 4590 測定方法で独立気泡率測定機器(Quantachrome,ULTRAPYC 1200e)装備を用いて各切片の独立気泡率を測定し、その結果を下記の表1に記載した。 The closed cell ratio of each of the specimens (N 1 to N 9 ) was measured using a closed cell ratio measuring device (Quantachrome, ULTRAPYC 1200e) according to the KS M ISO 4590 measurement method, and the results are shown in Table 1 below.

そして、d1は、発泡体の全体厚に対する、前記第1表層部(N)から最小独立気泡率を有する切片(Nmin)までの厚さ(=N~Nmin厚さ)の比率(d1=N~Nminの厚さ/発泡体の全体厚)であり、d2は、発泡体の全体厚に対する、前記第2表層部(N)から最小独立気泡率を有する切片(Nmin)までの厚さ(=N~Nmin厚さ)の比率(d2=N~Nminの厚さ/発泡体の全体厚)を意味する。このとき、前記発泡体の全体厚は、面材が付着していた発泡体の両表面をそれぞれ5mmずつ切断した後の発泡体の厚さを意味する。そして、前記N~Nminの厚さ及びN~Nminの厚さは、図1に示すように、前記第1表層部の上部面又は前記第2表層部の下部面から最小独立気泡率を有する切片(Nmin)の厚さ方向の1/2地点までの垂直距離を意味する。すなわち、d1は、第1表層部(N)の上部面路から最小独立気泡率を有する切片(Nmin)の1/2地点までの厚さ/発泡体の全体厚、d2は、第2表層部(N)の下部面路から最小独立気泡率を有する切片(Nmin)の1/2地点までの厚さ/発泡体の全体厚を意味する。 d1 is the ratio of the thickness (=N 1 to N min thickness) from the first surface layer portion (N 1 ) to the slice (N min ) having the minimum closed cell ratio to the total thickness of the foam (d1=N 1 to N min thickness/total foam thickness), and d2 is the ratio of the thickness (=N 9 to N min thickness) from the second surface layer portion (N 9 ) to the slice (N min ) having the minimum closed cell ratio to the total thickness of the foam (d2=N 9 to N min thickness/total foam thickness). In this case, the total thickness of the foam refers to the thickness of the foam after cutting off both surfaces of the foam to which the facing material was attached by 5 mm. The thicknesses N 1 to N min and N 9 to N min refer to the vertical distance from the upper surface of the first surface layer portion or the lower surface of the second surface layer portion to a 1/2 point in the thickness direction of the section (N min ) having the minimum closed cell content, as shown in Fig. 1. That is, d1 refers to the thickness from the upper surface path of the first surface layer portion (N 1 ) to a 1/2 point of the section (N min ) having the minimum closed cell content / the total thickness of the foam, and d2 refers to the thickness from the lower surface path of the second surface layer portion (N 1 ) to a 1/2 point of the section (N min ) having the minimum closed cell content / the total thickness of the foam.

Figure 0007573109000001
Figure 0007573109000001

実験例2:圧縮強度
実施例及び比較例のフェノール発泡体を150mm(L)×150mm(W)×面材を含む発泡体の厚さどおりの試片に準備し、前記試片をLloyd instrument社のLF Plus万能材料試験機(Universal Testing Machine)の広い板の間に置いて、UTM装備で試片の厚さの10%mm/min速度で設定し、圧縮強度実験を開始して、厚さが減少する間に示される第一圧縮降伏点での強度を記録した。圧縮強度は、KS M ISO 844規格の方法で測定しており、その結果を下記の表2に記載した。
Experimental Example 2: Compressive Strength The phenolic foams of the examples and comparative examples were prepared into specimens of 150 mm (L) x 150 mm (W) x the same thickness as the foam including the facing, and the specimens were placed between the wide plates of a Lloyd Instrument LF Plus Universal Testing Machine. The UTM equipment was set to a speed of 10% mm/min of the specimen thickness, and a compressive strength experiment was started. The strength at the first compressive yield point during the thickness reduction was recorded. The compressive strength was measured according to the method of KS M ISO 844 standard, and the results are shown in Table 2 below.

実験例3:撓み
図4は、本発明による面材を含むフェノール発泡体の撓み程度を測定する方法を簡略に示した模式図である。実施例及び比較例の面材を含むフェノール発泡体の表面が、床面に接するように偏平な床に置いた。そして、前記床面と接する前記フェノール発泡体表面の4角(頂点)地点と、床面からの間隔(p1,p2,p3,p4)を測定した。そして、フェノール発泡体の長さ方向の2辺と床面との間の間隔の最大隔離距離(r1,r2)を測定した。このとき、発泡体が床面と密着している場合、各々の間隔は、「0」となる。
Experimental Example 3: Deflection Figure 4 is a schematic diagram showing a simplified method for measuring the degree of deflection of a phenolic foam containing a facing material according to the present invention. The phenolic foam containing the facing material of the embodiment and the comparative example was placed on a flat floor so that the surface of the foam was in contact with the floor. The four corners (vertices) of the surface of the phenolic foam in contact with the floor and the distances (p1, p2, p3, p4) from the floor were measured. The maximum separation distances (r1, r2) between the two longitudinal sides of the phenolic foam and the floor were measured. At this time, when the foam is in close contact with the floor, each distance is "0".

そして、25℃、相対湿度60%の条件下で、7日間、前記フェノール発泡体を放置し、その後、フェノール発泡体の撓み程度を測定した。発泡体の表面部が床面に向かって凹に撓む場合(I)は、上記と同様の方法によって4本の角(頂点)地点と床面からの間隔(P1,P2,P3,P4)を測定し、下記の式1によってフェノール発泡体に撓みが発生した程度を表2に記載した。そして、発泡体の表面部が天井に向かって凸に撓む場合(II)は、フェノール発泡体の長さ方向の2辺と床面との間の間隔の最大隔離距離(R1,R2)を測定し、下記の式2によってフェノール発泡体に撓みが発生した程度を表2に記載した。 The phenolic foam was then left for 7 days under conditions of 25°C and 60% relative humidity, after which the degree of deflection of the phenolic foam was measured. In cases where the foam surface was bent concavely toward the floor (I), the distances (P1, P2, P3, P4) between the four corners (vertices) and the floor were measured using the same method as above, and the degree of deflection of the phenolic foam was recorded in Table 2 using the following formula 1. In cases where the foam surface was bent convexly toward the ceiling (II), the maximum separation distances (R1, R2) between the two longitudinal sides of the phenolic foam and the floor were measured, and the degree of deflection of the phenolic foam was recorded in Table 2 using the following formula 2.

[式1]
撓み発生程度(△S)=[|P1-p1|+|P2-p2|+|P3-p3|+|P4-p4|]/4
[Formula 1]
Degree of deflection (△S) = [|P1-p1| + |P2-p2| + |P3-p3| + |P4-p4|]/4

[式2]
撓み発生程度(△S’)=[|R1-r1|+|R2-r2|]/2
[Formula 2]
Degree of deflection (△S') = [|R1-r1| + |R2-r2|]/2

実験例4:寸法安定性
図4は、本発明のフェノール発泡体の寸法安定性を測定する方法を簡略に示した模式図である。
Experimental Example 4: Dimensional Stability FIG. 4 is a schematic diagram showing a simplified method for measuring the dimensional stability of the phenolic foam of the present invention.

実施例及び比較例のフェノール発泡体を100mm(L)×100mm(W)×面材を含む発泡体の厚さどおりの試片に準備した。そして、図5のように、試片の長さ(L)及び幅(W)方向において、均等なn(n=3)本地点に線を引いて、25℃で、前記個々の線の初期長さ(a)を測定した。 The phenolic foams of the examples and comparative examples were prepared into test pieces measuring 100 mm (L) x 100 mm (W) x the thickness of the foam including the facing. Then, as shown in Figure 5, lines were drawn at n (n = 3) equal points in the length (L) and width (W) directions of the test piece, and the initial length (a) of each line was measured at 25°C.

そして、前記試片を70℃のオーブンで48時間放置した後、各地点の以後長さ(a’)を測定し、初期寸法で変化した寸法変化率(%)を下記の式3によってそれぞれ測定し、その平均値を表2に記載した。寸法安定性は、KS M ISO 2796規格の方法で測定した。 The specimens were then left in an oven at 70°C for 48 hours, after which the length (a') at each point was measured, and the dimensional change rate (%) from the initial dimension was calculated using the following formula 3, and the average values are shown in Table 2. Dimensional stability was measured according to the method of KS M ISO 2796 standard.

[式3]
寸法変化率(%)=(|初期長さ(a)-以後長さ(a’)|/初期長さ(a))×100
[Formula 3]
Dimensional change rate (%) = (| initial length (a) - subsequent length (a') | / initial length (a)) x 100

上記式3において、前記初期長さ(a)は、発泡体の長さ(L)及び幅(W)方向において、均等なn本地点の各線の長さであり、前記以後長さ(a’)は、前記発泡体を70℃のオーブンで48時間放置した後、前記各地点の各線の以後長さ(a’)を意味する。このとき、nは、2~5であってもよい。 In the above formula 3, the initial length (a) is the length of each of n equal lines in the length (L) and width (W) directions of the foam, and the subsequent length (a') means the subsequent length (a') of each line at each of the points after the foam is left in an oven at 70°C for 48 hours. Here, n may be 2 to 5.

実験例5:初期熱伝導率
実施例及び比較例のフェノール樹脂発泡体を、いずれか表面から50mmとなるように切断し、300mm×300mmの大きさに切断して試片を準備し、前記試片を70℃で、12時間で乾燥して前処理した。そして、前記試片に対して、KS L 9016(平板熱流計法測定方法)の測定条件に従って、平均温度20℃で、HC-074-300(EKO社)熱伝導率機器を用いて熱伝導率を測定し、その結果を下記の表2に記載した。
Experimental Example 5: Initial thermal conductivity The phenolic resin foams of the examples and comparative examples were cut to 50 mm from either surface, and then cut into 300 mm x 300 mm pieces to prepare specimens, which were then pretreated by drying at 70° C. for 12 hours. The thermal conductivity of the specimens was measured using a thermal conductivity instrument HC-074-300 (EKO Co., Ltd.) at an average temperature of 20° C. according to the measurement conditions of KS L 9016 (plate heat flow meter measurement method), and the results are shown in Table 2 below.

実験例6:長期熱伝導率
実施例及び比較例のフェノール樹脂発泡体を、いずれか表面から50mmとなるように切断し、300mm×300mmの大きさに切断して試片を準備し、前記試片をEN13823に従って、70℃で、7日間乾燥した後、110℃で、14日間乾燥した後、平均温度20℃で、HC-074-300(EKO社)熱伝導率機器を用いて熱伝導率を測定し、その結果を下記の表2に記載した。
Experimental Example 6: Long-term thermal conductivity The phenolic resin foams of the Examples and Comparative Examples were cut to 50 mm from either surface, and then cut into 300 mm x 300 mm pieces to prepare test pieces. The test pieces were dried at 70°C for 7 days and then at 110°C for 14 days in accordance with EN13823, and the thermal conductivity was measured at an average temperature of 20°C using a thermal conductivity instrument HC-074-300 (EKO Co., Ltd.). The results are shown in Table 2 below.

Figure 0007573109000002
Figure 0007573109000002

上記表1に示すように、実施例のフェノール発泡体は、優れた圧縮強度と共に、撓み程度を充分抑制して、優れた熱伝導率を示すことが分かる。以上のように、本発明について例示の図面を参照して説明したが、本発明は、本明細書に開示の実施例と図面によって限定されるものではなく、本発明の技術思想の範囲内における通常の技術者によって様々な変形が行われることは明らかである。なお、本発明の実施例を前述しながら本発明の構成による作用効果を明示的に記載して説明しなかったとしても、当該構成によって予測可能な効果も認めるべきであることは当然である。 As shown in Table 1 above, the phenol foam of the embodiment exhibits excellent compressive strength, sufficient suppression of the degree of deflection, and excellent thermal conductivity. As described above, the present invention has been described with reference to the exemplary drawings, but the present invention is not limited to the embodiments and drawings disclosed in this specification, and it is clear that various modifications can be made by ordinary engineers within the scope of the technical concept of the present invention. Furthermore, even if the effects of the configuration of the present invention have not been explicitly described and explained while describing the embodiments of the present invention, it goes without saying that the effects that can be predicted by the configuration should also be recognized.

d1 発泡体の全体厚に対する、第1表層部(N)から最小独立気泡率を有する切片(Nmin)までの厚さ
d2 発泡体の全体厚に対する、第2表層部(N)から最小独立気泡率を有する切片(Nmin)までの厚さ
10 ノズルの吐出口
L 吐出口の長さ
W 吐出口の幅
3 面材
7 コンベヤー
100 フェノール発泡体
d1: Thickness from the first surface layer (N 1 ) to the section (N min ) having the minimum closed cell rate relative to the total thickness of the foam d2: Thickness from the second surface layer (N N ) to the section (N min ) having the minimum closed cell rate relative to the total thickness of the foam 10: Nozzle outlet L: Length of outlet W: Width of outlet 3: Face material 7: Conveyor 100: Phenol foam

Claims (4)

厚さが90mm~300mmであるフェノール発泡体であって、
前記発泡体のいずれか表面から、その表面に沿って厚さ方向にN(N≧7の奇数)本の厚さ10mm~30mmの切片に均分したとき、第1表層部(N)の独立気泡率は、第2表層部(N)の独立気泡率よりも低く、前記N本の切片のうち最小独立気泡率を有する切片(Nmin)は、前記第1表層部(N)と中間切片(N)との間に位置
前記第1表層部(N )の独立気泡率と、前記第2表層部(N )の独立気泡率との差は、0.1%~3%であり、
前記第1表層部(N )の独立気泡率と、前記第2表層部(N )の独立気泡率は、それぞれ85%以上であり、
前記最小独立気泡率を有する切片(N min )の独立気泡率は、70%以上であり、
前記第2表層部(N )が最大独立気泡率を有し、
前記第2表層部(N )と、前記最小独立気泡率を有する切片(N min )との独立気泡率の差は、1%~7%である、
フェノール発泡体。
A phenolic foam having a thickness of 90 mm to 300 mm ,
When the foam is evenly divided from any one surface into N (N≧7 odd number) slices having a thickness of 10 mm to 30 mm along the thickness direction from the surface, the closed cell ratio of a first surface layer portion (N 1 ) is lower than the closed cell ratio of a second surface layer portion (N N ), and a slice (N min ) having the smallest closed cell ratio among the N slices is located between the first surface layer portion (N 1 ) and an intermediate slice (N c );
a difference between the closed cell rate of the first surface layer portion (N 1 ) and the closed cell rate of the second surface layer portion (N N ) is 0.1% to 3%;
the closed cell rate of the first surface layer portion (N 1 ) and the closed cell rate of the second surface layer portion (N N ) are each 85% or more;
The closed cell ratio of the piece (N min ) having the minimum closed cell ratio is 70% or more;
The second surface layer portion (N N ) has a maximum closed cell ratio;
a difference in closed cell ratio between the second surface layer portion (N N ) and the piece (N min ) having the minimum closed cell ratio is 1% to 7%;
Phenolic foam.
前記発泡体の全体厚に対するd1とd2の比率は、0.2:0.8~0.45:0.55であり、
前記d1は、前記発泡体の全体厚に対する、前記第1表層部(N)から最小独立気泡率を有する切片(Nmin)までの厚さの比率であり、前記d2は、前記発泡体の全体厚に対する、前記第2表層部(N)から最小独立気泡率を有する切片(Nmin)までの厚さの比率である、
請求項1に記載のフェノール発泡体。
The ratio of d1 to d2 with respect to the total thickness of the foam is 0.2:0.8 to 0.45:0.55;
The d1 is a ratio of the thickness from the first surface layer portion (N 1 ) to the section (N min ) having the minimum closed cell ratio to the entire thickness of the foam, and the d2 is a ratio of the thickness from the second surface layer portion (N N ) to the section (N min ) having the minimum closed cell ratio to the entire thickness of the foam.
2. The phenolic foam of claim 1.
25℃、相対湿度60%の条件下、7日経過後の発泡体の撓みが0.1cm~0.7cmである、
請求項1又は2に記載のフェノール発泡体。
The deflection of the foam after 7 days under conditions of 25°C and 60% relative humidity is 0.1 cm to 0.7 cm.
The phenolic foam of claim 1 or 2.
EN13823に従って、70℃で、7日間乾燥した後、110℃で、14日間乾燥した後、平均温度20℃で測定した熱伝導率が0.018W/m・K~0.022W/m・Kである、
請求項1又は2に記載のフェノール発泡体。
A thermal conductivity of 0.018 W/m·K to 0.022 W/m·K measured at an average temperature of 20°C after drying at 70°C for 7 days and then at 110°C for 14 days in accordance with EN 13823;
The phenolic foam of claim 1 or 2.
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