JPH0363990B2 - - Google Patents

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Publication number
JPH0363990B2
JPH0363990B2 JP16469784A JP16469784A JPH0363990B2 JP H0363990 B2 JPH0363990 B2 JP H0363990B2 JP 16469784 A JP16469784 A JP 16469784A JP 16469784 A JP16469784 A JP 16469784A JP H0363990 B2 JPH0363990 B2 JP H0363990B2
Authority
JP
Japan
Prior art keywords
phenolic resin
foam
resol
phenol
uniform
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
Application number
JP16469784A
Other languages
Japanese (ja)
Other versions
JPS6142549A (en
Inventor
Kazuo Iwasaki
Hiroshi Kawakami
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.)
Achilles Corp
Original Assignee
Achilles Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Achilles Corp filed Critical Achilles Corp
Priority to JP16469784A priority Critical patent/JPS6142549A/en
Publication of JPS6142549A publication Critical patent/JPS6142549A/en
Publication of JPH0363990B2 publication Critical patent/JPH0363990B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】[Detailed description of the invention]

(発明の属する技術分野) 本発明は独立気泡を有し、均一な微細セル構造
を有するフエノール樹脂発泡体の製造方法に関す
る。 フエノール樹脂発泡体は、耐火性、断熱性など
の種々のすぐれた特性から各種用途に利用されて
いる。一般にフエノール樹脂発泡体の製造方法と
しては、ノボラツク型フエノール樹脂とヘキサメ
チレンテトラミンの混合物を用いる方法、レゾー
ル系フエノール樹脂に発泡剤、界面活性剤、酸性
硬化剤を配合した混合物を用いる方法等が知られ
ている。 本発明は、レゾール系フエノール樹脂を用いた
フエノール樹脂発泡体の製造方法に関するもので
ある。 (従来技術) レゾール系フエノール樹脂の製造は、一般に制
御された反応条件および制御された過剰量のアル
デヒド化合物の存在下で、フエノール化合物とア
ルデヒド化合物とを反応させることによつて製造
することができる。レゾール系フエノール樹脂に
一定量の発泡剤、整泡剤および酸性硬化剤を混合
させ、室温または40〜120℃の温度をかけること
によつて発泡を行う。 このようにして得られたフエノール樹脂発泡体
は、通常40〜100%の連続セルを有すると考えら
れる。これはセル壁の破壊及び発泡体中心部の裂
け目、ボイド等によつて生じるものである。上記
問題点を改良したものとして、特開昭56−30438
がある。これは、N−メチル−2−ピロリドンを
添加し、均一なセルを得るものである。 (解決すべき問題点) しかし、N−メチル−2−ピロリドン存在下で
得たフエノール樹脂発泡体はセルを均一微細にす
る効果は若干見られるが、連続セルが多数存在す
るものであつた。 そこで本発明者らは、独立気泡を有し、均一微
細なセル構造を持つ、フエノール樹脂発泡体を得
るべく鋭意研究した結果、整泡剤としてポリオキ
シエチレンポリオキシアルキレンリシノール酸エ
ーテルを特定の割合にて混合することにより、本
発明の目的とするフエノール樹脂発泡体が得られ
ることを見い出したものである。 (発明の構成) すなわち、本発明はレゾール系フエノール樹
脂、発泡剤、整泡剤、硬化剤などからフエノール
樹脂発泡体を製造するに当り、整泡剤としてポリ
オキシエチレンポリオキシアルキレンリシノール
酸エーテルをレゾール系フエノール樹脂100重量
部に対して0.1〜10重量部添加することを特徴と
するフエノール樹脂発泡体の製造方法である。 本発明に使用するポリオキシエチレンポリオキ
シアルキレンリシノール酸エーテルは次の構造式
で示される。 n=10〜50 m=5〜20 n≧m+5 R=プロピレン又はブチレン エチレンオキシド及びアルキレンオキシドの付
加量により親水性、疎水性の強さのバランス
(HLB)は変わるが、本発明に使用するポリオキ
シエチレンポリオキシアルキレンリシノール酸エ
ーテルのHLBは、レゾール系フエノール樹脂の
種類により異なるが、8.5〜17.5好ましくは10〜
15が良い。 又この整泡剤の使用量としては、レゾール系フ
エノール樹脂100重量部に対して0.1〜10重量部好
ましくは0.5〜5重量部が良い。10重量部をこえ
た場合独立気泡の微細セル構造を持つフオームに
なるが機械強度、耐熱性、耐火性の低下があるの
で好ましくない。0.1重量部未満の場合、独立気
泡の均一な微細セル構造を持つフオームが得られ
ない。 レゾール系フエノール樹脂の製造に使用するフ
エノール化合物またはアルデヒド化合物として
は、種々の化合物を使用することができる。フエ
ノール化合物にはフエノール並びにクレゾールお
よびキシレノールのようなその同族体あるいはこ
れらの化合物の混合物の両方が含まれる。フエノ
ール化合物と反応するアルデヒド化合物には、例
えばホルムアルデヒド、アセトアルデヒド、フル
ブラール、および他のアルデヒドならびにこれら
の化合物の混合物が含まれる。さらに、アルデヒ
ド生成性化合物を用いることもでき、例えばパラ
ホルムアルデヒド、ヘキサメチレンテトラミン、
メチロール、トリオキサン、テトラオキシメタン
およびその他のようなホルムアルデヒドに分解す
る化合物ならびにこれらの化合物の混合物も使用
することができる。 フエノール以外のフエノール系化合物とホルム
アルデヒドまたはその複合体形以外のアルデヒド
との反応はフエノールとホルムアルデヒドとの反
応より遅い。従つて本発明では、フエノールとホ
ルムアルデヒドを反応させたレゾール系フエノー
ル樹脂を用いることが好ましい。 本発明に使用できる発泡剤としては、沸点が約
−40℃〜100℃の塩素化および沸素化炭化水素、
例えばクロロホルム、塩化メチレン、トリクロロ
フルオロメタン、テトラフルオロメタン、1.1.2
−トリクロロ−1.2.2−トリフルオロエタン、モ
ノクロロジフルオロメタン、ジクロロジフルオロ
メタン、1.1−ジクロロ−1.2.2.2−テトラフルオ
ロエタン、1.2−ジクロロ−1.1.2.2−テトラフル
オロエタン、1.1.1−トリクロロ−2.2.2−トリフ
ルオロエタン、1.2−ジフルオロエタン、ブロモ
トリフルオロエタン、1.1.2.2−テトラクロロ−
1.2−ジフルオロエタン、1.1.1.2−テトラクロロ
−2.2−ジフルオロエタンあるいはこれらの化合
物の混合物が含まれる。 本発明に使用される硬化剤としては、硫酸、塩
酸、リン酸等の鉱酸や、P−トルエンスルホン
酸、フエノールスルホン酸に代表される有機酸が
用いられ、これらを添加することによつてアルカ
リ性もしくは中性のレゾール系フエノール樹脂の
PHを一挙に酸性側に移行することにより、速やか
に縮合がはじまり、前記発泡剤の存在下で発泡が
始まる。 本発明のポリオキシエチレンポリオキシアルキ
レンリシノール酸エーテルは、レゾール系フエノ
ール樹脂にあらかじめ混入して使用する方法が好
ましい。ポリオキシエチレンポリオキシアルキレ
ンリシノール酸エーテルを混入するレゾール系フ
エノール樹脂及びその他の原料を混合、発泡する
には、反応混合物を均一に混合できる方法ならば
如何なる方法によつても良い。例えば1500〜
10000rpmのギヤ型またはビン型混合器のような
公知の混合装置で得ることができる。 (発明の効果) 本発明によつて得られるフエノール樹脂発泡体
の特徴は下記のとおりである。 (1) 従来のレゾール系フエノール樹脂発泡体に比
べ独立気泡率が高く、優れた断熱性能を示す。 (2) 発泡中心部の裂け目、ボイドがなく、均一な
微細セル構造を持つのでフオームの機械強度が
高い。 (3) フオーム発泡、硬化への影響が少なく、通常
の方法で発泡が可能である。 (4) 従来のフエノール樹脂発泡体と同等の難燃
性、低発煙性、耐熱性を持つ。 以上のごとく本発明によるレゾール系フエノー
ル樹脂発泡体は、独立気泡を有し、均一微細なセ
ル構造を持ち断熱性、耐熱性、難燃性に優れるこ
とから広く建材分野に使用することができる。 (実施例及び比較例) 次に実施例により本発明を具体的に説明するが
本発明はこの実施例に限定されるものではない。 実施例 1、2 第1表に示す反応混合物を1のポリエチレン
ビーカー中に秤量し、室温(20〜25℃)中でミキ
サー(回転数8000rpm)で10〜30秒間激しく撹拌
し、50℃〜80℃に加熱してある上部開放のアルミ
ニウム製モールド中で発泡させ、80℃〜120℃の
オーブン内で約10分間キユアーした後レゾール系
フエノール樹脂発泡体を得た。室温で2週間脱水
した後、フオーム物性を測定した。整泡剤として
シリコーン系界面活性剤を使用した比較例−1と
比べ、独立気泡率が高くなり、熱伝導率も低下し
た。また目視の結果発泡体中心部に裂け目もな
く、大きなボイドもなく、均一で微細なセル構造
であつた。 実施例 3、4 表−1に示す混合物を実施例−1と同様にして
レゾール系フエノール樹脂フオームを得た。 比較例−2と比べ、独立気泡率が高くなつた。
又、150℃の耐熱性も良好であつた。目視の結果
セル構造は均一で微細であつた。 実施例 5、6 表−1に示す混合物を実施例−1と同様にして
レゾール系フエノール樹脂フオームを得た。独立
気泡率が高く、セル構造の均一微細なフオームで
あつた。 比較例 1 表−1に示す混合物から得られたレゾール系フ
エノール樹脂フオームは、実施例1、2に比較し
て独立気泡率が低いだけでなく、目視の結果大き
なセルもみられ、セル構造が不均一であつた。 比較例 2 表−1に示す混合物から得られたレゾール系フ
エノール樹脂フオームは、独立気泡が全くなかつ
ただけでなく、セル構造も不均一であつた。 比較例 3 整泡剤としてN−メチル−2−ピロリドンを併
用した結果セル構造は均一微細になつたが、独立
気泡の増加はなかつた。
(Technical field to which the invention pertains) The present invention relates to a method for producing a phenolic resin foam having closed cells and a uniform fine cell structure. Phenol resin foams are used for various purposes due to their excellent properties such as fire resistance and heat insulation. In general, methods for producing phenolic resin foam include a method using a mixture of novolac type phenolic resin and hexamethylenetetramine, and a method using a mixture of resol type phenolic resin mixed with a blowing agent, a surfactant, and an acidic curing agent. It is being The present invention relates to a method for producing a phenolic resin foam using a resol-based phenolic resin. (Prior Art) Resol-based phenolic resins can generally be produced by reacting a phenolic compound and an aldehyde compound under controlled reaction conditions and in the presence of a controlled excess amount of the aldehyde compound. . Foaming is performed by mixing a certain amount of a foaming agent, a foam stabilizer, and an acidic curing agent with a resol type phenolic resin, and applying a temperature of room temperature or 40 to 120°C. The phenolic resin foam thus obtained is generally considered to have 40-100% open cells. This is caused by destruction of the cell walls and cracks, voids, etc. in the center of the foam. As an improvement on the above problems, JP-A-56-30438
There is. This involves adding N-methyl-2-pyrrolidone to obtain uniform cells. (Problems to be Solved) However, although the phenolic resin foam obtained in the presence of N-methyl-2-pyrrolidone had a slight effect of making the cells uniform and fine, there were many continuous cells. Therefore, the present inventors conducted extensive research to obtain a phenolic resin foam having closed cells and a uniform fine cell structure. It has been discovered that the phenolic resin foam which is the object of the present invention can be obtained by mixing in a . (Structure of the Invention) That is, the present invention uses polyoxyethylene polyoxyalkylene ricinoleic acid ether as a foam stabilizer when producing a phenolic resin foam from a resol type phenolic resin, a blowing agent, a foam stabilizer, a curing agent, etc. This is a method for producing a phenolic resin foam, characterized in that 0.1 to 10 parts by weight are added to 100 parts by weight of resol type phenolic resin. The polyoxyethylene polyoxyalkylene ricinoleic ether used in the present invention is represented by the following structural formula. n=10-50 m=5-20 n≧m+5 R=propylene or butylene The balance of hydrophilicity and hydrophobicity strength (HLB) changes depending on the amount of ethylene oxide and alkylene oxide added, but the polyoxylic acid used in the present invention The HLB of ethylene polyoxyalkylene ricinoleic acid ether varies depending on the type of resol type phenolic resin, but is 8.5 to 17.5, preferably 10 to
15 is good. The amount of the foam stabilizer to be used is preferably 0.1 to 10 parts by weight, preferably 0.5 to 5 parts by weight, per 100 parts by weight of the resol type phenolic resin. If the amount exceeds 10 parts by weight, a foam with a closed-cell fine cell structure will be formed, which is not preferable because mechanical strength, heat resistance, and fire resistance will decrease. When the amount is less than 0.1 part by weight, a foam having a uniform fine cell structure of closed cells cannot be obtained. Various compounds can be used as the phenol compound or aldehyde compound used in the production of the resol-based phenolic resin. Phenol compounds include both phenols and their congeners such as cresols and xylenol or mixtures of these compounds. Aldehyde compounds that react with phenolic compounds include, for example, formaldehyde, acetaldehyde, flubral, and other aldehydes and mixtures of these compounds. Furthermore, aldehyde-forming compounds can also be used, such as paraformaldehyde, hexamethylenetetramine,
Compounds that decompose to formaldehyde such as methylol, trioxane, tetraoxymethane and others and mixtures of these compounds can also be used. The reaction between a phenolic compound other than phenol and an aldehyde other than formaldehyde or its complex form is slower than the reaction between phenol and formaldehyde. Therefore, in the present invention, it is preferable to use a resol type phenol resin in which phenol and formaldehyde are reacted. Blowing agents that can be used in the present invention include chlorinated and fluorinated hydrocarbons with a boiling point of about -40°C to 100°C;
For example, chloroform, methylene chloride, trichlorofluoromethane, tetrafluoromethane, 1.1.2
-Trichloro-1.2.2-trifluoroethane, monochlorodifluoromethane, dichlorodifluoromethane, 1.1-dichloro-1.2.2.2-tetrafluoroethane, 1.2-dichloro-1.1.2.2-tetrafluoroethane, 1.1.1-trichloro-2.2 .2-trifluoroethane, 1.2-difluoroethane, bromotrifluoroethane, 1.1.2.2-tetrachloro-
Included are 1,2-difluoroethane, 1.1.1.2-tetrachloro-2,2-difluoroethane, or mixtures of these compounds. As the curing agent used in the present invention, mineral acids such as sulfuric acid, hydrochloric acid, and phosphoric acid, and organic acids such as P-toluenesulfonic acid and phenolsulfonic acid are used. Alkaline or neutral resol type phenolic resin
By shifting the pH to the acidic side all at once, condensation begins quickly, and foaming begins in the presence of the foaming agent. It is preferable that the polyoxyethylene polyoxyalkylene ricinoleic acid ether of the present invention is used by being mixed in advance with a resol type phenolic resin. Any method may be used for mixing and foaming the resol type phenolic resin containing polyoxyethylene polyoxyalkylene ricinoleic acid ether and other raw materials as long as the reaction mixture can be mixed uniformly. For example 1500~
It can be obtained with known mixing devices such as gear type or bottle type mixers at 10000 rpm. (Effects of the Invention) The characteristics of the phenolic resin foam obtained by the present invention are as follows. (1) Compared to conventional resol-based phenolic resin foams, it has a higher closed cell ratio and exhibits superior heat insulation performance. (2) There are no cracks or voids in the foam center, and the foam has a uniform fine cell structure, so the foam has high mechanical strength. (3) It has little effect on foam foaming and curing, and can be foamed using normal methods. (4) It has flame retardancy, low smoke emission, and heat resistance equivalent to conventional phenolic resin foam. As described above, the resol-based phenolic resin foam according to the present invention has closed cells, has a uniform fine cell structure, and has excellent heat insulation properties, heat resistance, and flame retardancy, and therefore can be widely used in the field of building materials. (Examples and Comparative Examples) Next, the present invention will be specifically explained with reference to Examples, but the present invention is not limited to these Examples. Examples 1 and 2 The reaction mixture shown in Table 1 was weighed into a polyethylene beaker (1), stirred vigorously for 10 to 30 seconds with a mixer (rotation speed: 8000 rpm) at room temperature (20 to 25°C), and then heated to a temperature of 50°C to 80°C. It was foamed in an aluminum mold with an open top heated to .degree. C. and cured in an oven at 80.degree. C. to 120.degree. C. for about 10 minutes to obtain a resol-based phenolic resin foam. After two weeks of dehydration at room temperature, the foam properties were measured. Compared to Comparative Example 1 in which a silicone surfactant was used as a foam stabilizer, the closed cell ratio was higher and the thermal conductivity was lower. Visual inspection revealed that there were no tears or large voids in the center of the foam, and it had a uniform and fine cell structure. Examples 3 and 4 A resol type phenol resin foam was obtained using the mixture shown in Table 1 in the same manner as in Example 1. Compared to Comparative Example-2, the closed cell ratio was higher.
Moreover, the heat resistance at 150°C was also good. Visual inspection revealed that the cell structure was uniform and fine. Examples 5 and 6 A resol type phenol resin foam was obtained using the mixture shown in Table 1 in the same manner as in Example 1. It had a high closed cell ratio and a uniform fine cell structure. Comparative Example 1 The resol type phenolic resin foam obtained from the mixture shown in Table 1 not only had a lower closed cell ratio than Examples 1 and 2, but also had large cells as a result of visual inspection, indicating that the cell structure was defective. It was uniform and warm. Comparative Example 2 The resol type phenolic resin foam obtained from the mixture shown in Table 1 not only had no closed cells at all, but also had a non-uniform cell structure. Comparative Example 3 As a result of using N-methyl-2-pyrrolidone as a foam stabilizer, the cell structure became uniform and fine, but the number of closed cells did not increase.

【表】【table】

【表】 表中の配合量数字は重量部を示す。 整泡剤−A:ポリオキシエチレンポリオキシプロ
ピレンリシノール酸エーテル(HLB=12) 整泡剤−B:ポリオキシエチレンポリオキシブチ
レンリシノール酸エーテル(HLB=12) フエノール樹脂−A:粘度が2500cp/25℃であ
り、固形分含有率が75%であるフエノール、
ホルムアルデヒド(レゾール系フエノール)
樹脂 フエノール樹脂−B:粘度が1000cp/25℃であ
り、固形分含有率が75%であるフエノール、
ホルムアルデヒド(レゾール系フエノール)
樹脂 シリコーン系界面活性剤(整泡剤):トーレシリ
コーン製SH−193 発泡剤:トリクロロトリフルオロエタン 硬化剤:65%フエノールスルホン酸水溶液 フオーム密度:JISA−9514により測定 圧縮強度:JISA−9514により測定 脆性:ASTMC−421により測定値が小さい程フ
オームは脆くない。 独立気泡率:ASTMD−2856により測定 熱伝導率:JISA−9514により測定 発煙係数:220×220×30mmの試験片を使用して
JISA−1321の難燃2級Aの表面試験により
測定 値が小さい程発煙量は少ない。 耐熱性:100×100×50mmの試験片を150℃のオー
ブン中で24時間放置し、変形、亀裂等を測定
する。 変形が少なく、亀裂のないものをOKとす
る。
[Table] The blending amount numbers in the table indicate parts by weight. Foam stabilizer-A: Polyoxyethylene polyoxypropylene ricinoleate ether (HLB=12) Foam stabilizer-B: Polyoxyethylene polyoxybutylene ricinoleate ether (HLB=12) Phenol resin-A: Viscosity is 2500 cp/25 phenol, whose solid content is 75%
Formaldehyde (resole phenol)
Resin Phenol Resin-B: Phenol with a viscosity of 1000 cp/25°C and a solid content of 75%,
Formaldehyde (resole phenol)
Resin silicone surfactant (foam stabilizer): Toray Silicone SH-193 Foaming agent: Trichlorotrifluoroethane Curing agent: 65% phenolsulfonic acid aqueous solution Foam density: Measured according to JISA-9514 Compressive strength: Measured according to JISA-9514 Brittleness: The smaller the measured value according to ASTMC-421, the less brittle the foam is. Closed cell ratio: Measured according to ASTMD-2856 Thermal conductivity: Measured according to JISA-9514 Smoke emission coefficient: Using a 220 x 220 x 30 mm test piece
According to the JISA-1321 flame retardant grade 2 A surface test, the smaller the measured value, the lower the amount of smoke emitted. Heat resistance: Leave a 100 x 100 x 50 mm test piece in an oven at 150°C for 24 hours and measure deformation, cracks, etc. Items with little deformation and no cracks are acceptable.

Claims (1)

【特許請求の範囲】[Claims] 1 レゾール系フエノール樹脂、発泡剤、整泡
剤、硬化剤などからフエノール樹脂発泡体を製造
するに当り、整泡剤としてポリオキシエチレンポ
リオキシアルキレンリシノール酸エーテルをレゾ
ール系フエノール樹脂100重量部に対して0.1〜10
重量部添加することを特徴とするフエノール樹脂
発泡体の製造方法。
1. When producing phenolic resin foam from resol-based phenolic resin, blowing agent, foam stabilizer, curing agent, etc., polyoxyethylene polyoxyalkylene ricinoleic acid ether is added as a foam stabilizer to 100 parts by weight of resol-based phenolic resin. 0.1~10
A method for producing a phenolic resin foam, which comprises adding parts by weight.
JP16469784A 1984-08-06 1984-08-06 Production of phenolic resin foam Granted JPS6142549A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16469784A JPS6142549A (en) 1984-08-06 1984-08-06 Production of phenolic resin foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16469784A JPS6142549A (en) 1984-08-06 1984-08-06 Production of phenolic resin foam

Publications (2)

Publication Number Publication Date
JPS6142549A JPS6142549A (en) 1986-03-01
JPH0363990B2 true JPH0363990B2 (en) 1991-10-03

Family

ID=15798149

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16469784A Granted JPS6142549A (en) 1984-08-06 1984-08-06 Production of phenolic resin foam

Country Status (1)

Country Link
JP (1) JPS6142549A (en)

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US8850477B2 (en) 1995-10-02 2014-09-30 Starsight Telecast, Inc. Systems and methods for linking television viewers with advertisers and broadcasters
US8869204B2 (en) 1996-05-03 2014-10-21 Starsight Telecast, Inc. Method and system for displaying advertisements in an electronic program guide
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US8918807B2 (en) 1997-07-21 2014-12-23 Gemstar Development Corporation System and method for modifying advertisement responsive to EPG information
US9015749B2 (en) 1997-07-21 2015-04-21 Rovi Guides, Inc. System and method for modifying advertisement responsive to EPG information
US9191722B2 (en) 1997-07-21 2015-11-17 Rovi Guides, Inc. System and method for modifying advertisement responsive to EPG information
US9591251B2 (en) 1997-10-06 2017-03-07 Rovi Guides, Inc. Interactive television program guide system with operator showcase
US9015750B2 (en) 1998-05-15 2015-04-21 Rovi Guides, Inc. Interactive television program guide system for determining user values for demographic categories
US9172987B2 (en) 1998-07-07 2015-10-27 Rovi Guides, Inc. Methods and systems for updating functionality of a set-top box using markup language
US9226006B2 (en) 1998-07-14 2015-12-29 Rovi Guides, Inc. Client-server based interactive guide with server recording
US9021538B2 (en) 1998-07-14 2015-04-28 Rovi Guides, Inc. Client-server based interactive guide with server recording
US9118948B2 (en) 1998-07-14 2015-08-25 Rovi Guides, Inc. Client-server based interactive guide with server recording
US9232254B2 (en) 1998-07-14 2016-01-05 Rovi Guides, Inc. Client-server based interactive television guide with server recording
US9055319B2 (en) 1998-07-14 2015-06-09 Rovi Guides, Inc. Interactive guide with recording
US9055318B2 (en) 1998-07-14 2015-06-09 Rovi Guides, Inc. Client-server based interactive guide with server storage
US9426509B2 (en) 1998-08-21 2016-08-23 Rovi Guides, Inc. Client-server electronic program guide
US8931008B2 (en) 1999-06-29 2015-01-06 United Video Properties, Inc. Promotional philosophy for a video-on-demand-related interactive display within an interactive television application
US8904441B2 (en) 2003-11-06 2014-12-02 United Video Properties, Inc. Systems and methods for providing program suggestions in an interactive television program guide
US9113107B2 (en) 2005-11-08 2015-08-18 Rovi Guides, Inc. Interactive advertising and program promotion in an interactive television system
US9215504B2 (en) 2006-10-06 2015-12-15 Rovi Guides, Inc. Systems and methods for acquiring, categorizing and delivering media in interactive media guidance applications
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US9125169B2 (en) 2011-12-23 2015-09-01 Rovi Guides, Inc. Methods and systems for performing actions based on location-based rules
US9288521B2 (en) 2014-05-28 2016-03-15 Rovi Guides, Inc. Systems and methods for updating media asset data based on pause point in the media asset

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