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JPH0463992B2 - - Google Patents
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JPH0463992B2 - - Google Patents

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Publication number
JPH0463992B2
JPH0463992B2 JP59277613A JP27761384A JPH0463992B2 JP H0463992 B2 JPH0463992 B2 JP H0463992B2 JP 59277613 A JP59277613 A JP 59277613A JP 27761384 A JP27761384 A JP 27761384A JP H0463992 B2 JPH0463992 B2 JP H0463992B2
Authority
JP
Japan
Prior art keywords
pressure
foam
urethane foam
container
hard urethane
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 - Lifetime
Application number
JP59277613A
Other languages
Japanese (ja)
Other versions
JPS61153481A (en
Inventor
Kazuto Uekado
Kazuo Okada
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.)
Takeda Pharmaceutical Co Ltd
Panasonic Holdings Corp
Original Assignee
Matsushita Refrigeration Co
Takeda Chemical Industries Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Refrigeration Co, Takeda Chemical Industries Ltd filed Critical Matsushita Refrigeration Co
Priority to JP59277613A priority Critical patent/JPS61153481A/en
Publication of JPS61153481A publication Critical patent/JPS61153481A/en
Publication of JPH0463992B2 publication Critical patent/JPH0463992B2/ja
Granted legal-status Critical Current

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  • Refrigerator Housings (AREA)

Description

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

産業上の利用分野 本発明は、冷蔵庫、冷凍プレハブ等に利用する
断熱体に関するものである。 従来の技術 第4図は、本発明の断熱体を示している。以下
に従来例の構成について第4図を参考に説明す
る。 近年、断熱箱体の断熱性能を図る目的で内部を
減圧した断熱体を用いることが注目されている。
この断熱体の心材としては、パーライト等の粉
末、ハニカム、及び発泡体等が用いられる。例え
ば、特開昭57−133870号に示されるように連続気
泡を有する硬質ウレタンフオームを心材とする提
案がなされている。特開昭57−13870号を第4図
で説明すると、図において、1は断熱性構造体で
あり、連続気泡を有する硬質ウレタンフオーム2
を気密性薄膜から成る容器3で被い、内部を
0.001mmHgまで減圧し、密閉している。硬質ウレ
タンフオーム2は、独立気泡率が約80〜90%程度
の市販の材料を高温高湿下で真空脱気して、気泡
膜を破り、連続気泡を得ることが特徴となつてい
る。 発明が解決しようとする問題点 しかし、このような断熱性構造体においては、
硬質ウレタンフオーム2の気泡膜は、高温高湿下
の状態でも、樹脂強度が強いため、破泡しない場
合があり、そのため、連続気泡率が100%に到達
しえないことが考えられる。このため初期の熱伝
導率が優れたものでも、経済時に断熱性構造体1
の内部圧力は、独立気泡部から徐々に拡散する空
気・水蒸気・フロンガス等の気体により上昇し、
熱伝導率が大きくなつてくるのである。例えば、
30cm×30cm×2cm(容積1800cm3)の大きさで、平
均気泡径100μm程度の硬質ウレタンフオーム2
の心材を有する断熱構造体1において、98%の連
続気泡率のとき、0.001mmHgまで減圧したとして
も、理論上2%の独立い気泡部に含まれる約36cm3
の気体(1800cm3×0.02)は、気泡膜の拡散抵抗を
受けながら徐々に減圧されている連続気泡部に拡
散する。実験によると圧力平衡に完全に達するの
に常温で約30日間、硬質ウレタンフオーム2の耐
熱温度に近い80〜100℃の雰囲気でも1〜3日間
の経時が必要であつた。そして、前記の約36cm3
気体が、究極的に内部圧力を0.001mmHgから15mm
Hgまで上昇させて熱伝導率を、0.020Kcal/mh
℃以上に劣化させることが考えられる。 これを防ぐには、少なくとも80〜100℃に断熱
性構造体1を維持し1日以上真空ポンプで排気し
続けることが必要であろう。すなわち、この操作
により、独立気泡部に残存する気体は気泡膜を介
して排気され、たとえ、独立気泡部があつたとし
ても所定の圧力まで減圧することができる。しか
しながら、この操作は、生産においては、排気設
備1台に対し、1日1体しか製造できず、量産化
は、非常に困難である。又高温高湿処理も大規模
な設備が必要となり、同様に量産化に対し、問題
である。 本発明は、上記問題点に鑑み、短時間の排気で
所定の圧力まで減圧できることによつて生産性を
大巾に向上させると共に、断熱体の断熱性能を長
期にわたつて維持し、品質の信頼性を確立するこ
とを目的とする。 問題点を解決するための手段 本発明の断熱体の製造方法は、上記問題点を解
決するために、100%未満60%以上の連続気泡率
を有する硬質ウレタンフオームからなる発泡体を
圧力容器内で5Kg/cm2以上の圧力で加圧して発泡
体の独立気泡を破泡し、この破泡した断熱体を金
属−プラスチツクラミネートフイルムからなる容
器内に収納して内部を減圧したのち、容器を密閉
してなるものである。 作 用 上記構成のように加圧によつて発泡体の気泡膜
を破り、連続気泡率を100%とした心材を金属−
プラスチツクスラミネートフイルムから成る容器
で被い内部を減圧するため、短時間の排気で断熱
体の内部圧力を均一に所定圧力まで減圧できると
共に、独立気泡部がないため長期間にわたつて内
部圧力の上昇がなく、初期の断熱性能を維持する
のである。 実施例 以下、本発明の一実施例を第1図〜第3図を参
考に説明する。 図において、4は下表に示す原料を用いて発泡
し硬化させた硬質ウレタンフオームからなる発泡
体(以下硬質ウレタンフオームと呼ぶ)で、常温
でエージングした後、所定の大きさに切断したも
のである。
INDUSTRIAL APPLICATION FIELD The present invention relates to a heat insulator used in refrigerators, frozen prefabricated products, and the like. BACKGROUND OF THE INVENTION FIG. 4 shows a heat insulating body of the present invention. The configuration of the conventional example will be explained below with reference to FIG. 4. In recent years, attention has been paid to the use of a heat insulator with a reduced internal pressure for the purpose of improving the heat insulation performance of a heat insulating box.
As the core material of this heat insulating body, powder such as perlite, honeycomb, foam, etc. are used. For example, as shown in JP-A-57-133870, a proposal has been made to use a hard urethane foam having open cells as the core material. To explain JP-A-57-13870 with Figure 4, in the figure 1 is a heat insulating structure, 2 is a rigid urethane foam having open cells.
is covered with a container 3 made of an airtight thin film, and the inside is sealed.
The pressure is reduced to 0.001mmHg and it is sealed. The hard urethane foam 2 is characterized in that a commercially available material with a closed cell ratio of about 80 to 90% is vacuum degassed under high temperature and high humidity to break the cell membrane and obtain open cells. Problems to be solved by the invention However, in such a heat-insulating structure,
The cell membrane of the hard urethane foam 2 has strong resin strength even under high temperature and high humidity conditions, so the cells may not burst, and it is conceivable that the open cell rate may not reach 100%. Therefore, even if the initial thermal conductivity is excellent, the thermal insulation structure 1
The internal pressure increases due to gases such as air, water vapor, and chlorofluorocarbon gas that gradually diffuse from the closed cell portion.
Thermal conductivity increases. for example,
Hard urethane foam 2 with a size of 30 cm x 30 cm x 2 cm (volume 1800 cm 3 ) and an average cell diameter of about 100 μm.
In the heat insulating structure 1 having a core material of
The gas (1800cm 3 ×0.02) diffuses into the open cell part, where the pressure is gradually reduced while being affected by the diffusion resistance of the cell membrane. According to experiments, it took about 30 days at room temperature to completely reach pressure equilibrium, and 1 to 3 days even in an atmosphere of 80 to 100°C, which is close to the heat resistance temperature of the rigid urethane foam 2. Then, the aforementioned approximately 36cm3 of gas will ultimately increase the internal pressure from 0.001mmHg to 15mm
Increase the thermal conductivity to 0.020Kcal/mh by increasing the temperature to Hg.
It is conceivable that the temperature may deteriorate above ℃. To prevent this, it will be necessary to maintain the heat insulating structure 1 at a temperature of at least 80 to 100°C and continue to evacuate it with a vacuum pump for one day or more. That is, by this operation, the gas remaining in the closed cell portion is exhausted through the cell membrane, and even if there is a closed cell portion, the pressure can be reduced to a predetermined pressure. However, in production, only one unit of exhaust equipment can be manufactured per day using this operation, and mass production is extremely difficult. Furthermore, high temperature and high humidity treatment also requires large-scale equipment, which is also a problem for mass production. In view of the above problems, the present invention greatly improves productivity by reducing the pressure to a predetermined pressure in a short time, maintains the insulation performance of the heat insulator over a long period of time, and improves quality reliability. The purpose is to establish gender. Means for Solving the Problems In order to solve the above-mentioned problems, the method for manufacturing a heat insulating body of the present invention is to produce a foam made of a hard urethane foam having an open cell ratio of less than 100% and 60% or more in a pressure vessel. Pressure is applied to the foam at a pressure of 5 kg/cm2 or more to burst the closed cells of the foam, and the burst insulation is placed in a container made of metal-plastic laminate film, the inside is depressurized, and the container is opened. It is sealed. Effect As shown in the above structure, the cell membrane of the foam is broken by pressurization, and the core material with an open cell ratio of 100% is made of metal.
Since the internal pressure is reduced by covering the container with a plastic laminate film, the internal pressure of the insulation can be uniformly reduced to the specified pressure with a short evacuation, and since there is no closed cell part, the internal pressure can be reduced for a long period of time. There is no rise, and the initial insulation performance is maintained. Embodiment Hereinafter, an embodiment of the present invention will be described with reference to FIGS. 1 to 3. In the figure, 4 is a foam made of hard urethane foam (hereinafter referred to as hard urethane foam) that is foamed and hardened using the raw materials shown in the table below, and is cut into a predetermined size after being aged at room temperature. be.

【表】【table】

【表】 表において、ポリオールは、芳香族ジアミンを
開始剤としてプロピレンオキサイド(以下、PO
と呼ぶ)を付加重合させて得た水酸基価442mg
KOH/gのポリエーテルポリオールである。整
泡剤は、信越化学製のシリコーン系界面活性剤、
F−335、発泡剤は、昭和電工(株)製フロンR−11、
触媒は、ジメチルエタノールアミンである。気泡
連通化剤は日本油脂(株)製ステアリン酸カルシウム
である。有機ポリイソシアネートは、日本ポリウ
レタン(株)製アミン当量136の粗製ジフエニ−ルメ
タンジイソシアネートである。これらの原料を
種々組合せて発泡を行ない、前記硬質ウレタンフ
オーム4を得、この後、圧力容器5中に硬質ウレ
タンフオーム4を配置し、圧力容器5中を0.01
Kg/cm2に減圧、及び2、3、4、5Kg/cm2までそ
れぞれ加圧し圧力処理硬質ウレタンフオーム6を
得た、この一部を実施例として、No.1〜No.3に示
し、比較例としてNo.A〜Bに表に示した。又、硬
質ウレタンフオーム4の密度連続気泡率と圧力処
理硬質ウレタンフオーム6の連続気泡率も表に示
す。この後、5Kg/cm2まで加圧したものを120℃
で約2時間、加熱し吸着水分を蒸発させて、アル
ミ蒸着ポリエステルフイルムとポリエチレンフイ
ルムのラミネート構成による金属−プラスチツク
スラミネートフイルムから成る容器7で被い、内
部を0.05mmHgまで減圧し、密閉して断熱体8を
得た。このときの排気時間は3分間であつた。得
られた断熱体8の密閉直後の初期値の熱伝導率と
30日後の熱伝導率も表に示した。なお、市販のフ
エノールフオームについても同様の実験を行な
い、結果を実施例No.4として表に付記した。 表から明らかなように、連続気泡率は、加圧処
理を行なうことにより、増加し、5Kg/cm2程度で
100%化することが判つた。これは、独立気泡中
の圧力が少なくとも1Kg/cm2に対し5Kg/cm2以上
の圧力をかけることにより、全ての気泡膜が耐え
切れず破泡するからである。ただし、独立気泡が
40%以上占める硬質ウレタンフオーム4の場合は
変形・収縮が起こる。これは1つ1つの気泡膜と
いう局所に応力がかかるのではなく、連なつた独
立気泡に応力がかかる確率が増加し、硬質ウレタ
ンフオーム4の広い部分に応力がかかる結果、ウ
レタンフオーム4は収縮・変形・破壊が起るもの
と考えられる。 そして、この連続気泡率が100%で独立気泡部
のない圧力処理をした硬質ウレタンフオーム6を
断熱体8の心材として用いるため、短時間の排気
で断熱体7の内部圧力を連続気泡を通して均一に
所定圧力まで減圧でき、量産効率の優れたものと
なる。又、気体を含有する独立気泡部がないため
断熱体7を長期にわたつて放置しても独立気泡部
からのガス拡散はなく、圧力上昇を起こすことは
ない。よつて、断熱体7の断熱性能は、長期にわ
たつて劣化することがなく品質の確保に寄与する
ものである。 発明の効果 本発明は、上記の説明から明らかなように以下
に示すような効果が得られるのである。 (a) 100%未満60%以上の連続気泡率を有する発
泡体を圧力容器中に配置し、加圧気体により加
圧することにより、連続気泡率を100%化した
ものであるから、これを金属−プラスチツクス
ラミネートフイルムから成る容器で被い内部を
減圧すると内部圧力は均一に所定圧力まで短時
間に到達することができ、量産時の生産性を確
保しうる。 (b) また、発泡体を圧力容器中で加圧して形成す
るので、独立気泡の壁を破泡しやすく、かつ圧
力が加え易いので連続気泡率100%が簡単に得
られるものであるとともに、圧力のみで破泡す
るので、破泡のために別途水分やアルカリを用
いて高温度状態から乾燥をさせる必要がないも
のである。すなわち、高温度の状態におかれた
発泡体では経時変化によつて密閉容器内部圧力
を高めてしまう可能性があるものが、圧力を加
えているだけなので発泡体を乾燥させたとして
も短時間ですむものである。 (c) 気体を含有する独立気泡部がないため、断熱
体を長期にわたつて放置しても独立気泡部から
のガス拡散はなく圧力上昇を起こすことはな
い、よつて断熱体の断熱性能は劣化することな
く品質の安定性を確保するものである。
[Table] In the table, polyols are produced using propylene oxide (hereinafter referred to as PO) using an aromatic diamine as an initiator.
Hydroxyl value 442mg obtained by addition polymerization of
KOH/g polyether polyol. The foam stabilizer is a silicone surfactant manufactured by Shin-Etsu Chemical.
F-335, the blowing agent is Freon R-11 manufactured by Showa Denko Co., Ltd.
The catalyst is dimethylethanolamine. The bubble communication agent is calcium stearate manufactured by Nippon Oil & Fats Co., Ltd. The organic polyisocyanate was crude diphenylmethane diisocyanate with an amine equivalent weight of 136 manufactured by Nippon Polyurethane Co., Ltd. Various combinations of these raw materials are foamed to obtain the hard urethane foam 4. Thereafter, the hard urethane foam 4 is placed in the pressure vessel 5, and the inside of the pressure vessel 5 is heated to 0.01.
A pressure-treated hard urethane foam 6 was obtained by reducing the pressure to Kg/cm 2 and increasing the pressure to 2, 3, 4, and 5 Kg/cm 2 , some of which are shown in Examples No. 1 to No. 3, Comparative examples are shown in Nos. A to B in the table. The table also shows the density open cell ratio of the hard urethane foam 4 and the open cell ratio of the pressure-treated hard urethane foam 6. After this, the product was pressurized to 5Kg/cm 2 and heated to 120℃.
The container was heated for about 2 hours to evaporate the adsorbed water, then covered with a container 7 made of a metal-plastic laminate film made of a laminate of an aluminum-deposited polyester film and a polyethylene film, and the inside was reduced to 0.05 mmHg and sealed. A heat insulator 8 was obtained. The evacuation time at this time was 3 minutes. The initial value of thermal conductivity of the obtained heat insulator 8 immediately after sealing and
The thermal conductivity after 30 days is also shown in the table. A similar experiment was conducted using commercially available phenol foam, and the results are added to the table as Example No. 4. As is clear from the table, the open cell ratio increases with pressure treatment and reaches approximately 5 kg/ cm2 .
It turned out to be 100%. This is because the pressure in closed cells is at least 1Kg/cm 2 , but when a pressure of 5Kg/cm 2 or more is applied, all the cell membranes cannot withstand the pressure and burst. However, closed cell
In the case of hard urethane foam 4, which accounts for 40% or more, deformation and shrinkage occur. This is because stress is not applied locally to each cell film, but the probability that stress is applied to a series of closed cells increases, and as a result, stress is applied to a wide area of the hard urethane foam 4, causing the urethane foam 4 to shrink. - It is thought that deformation and destruction may occur. Since this pressure-treated hard urethane foam 6 with a 100% open cell ratio and no closed cell portions is used as the core material of the heat insulator 8, the internal pressure of the heat insulator 7 can be uniformly maintained through the open cells by short-time evacuation. The pressure can be reduced to a predetermined pressure, resulting in excellent mass production efficiency. Further, since there is no closed cell portion containing gas, even if the heat insulator 7 is left for a long period of time, there will be no gas diffusion from the closed cell portion, and no pressure increase will occur. Therefore, the heat insulating performance of the heat insulator 7 does not deteriorate over a long period of time and contributes to ensuring quality. Effects of the Invention As is clear from the above description, the present invention provides the following effects. (a) A foam with an open cell ratio of less than 100% and 60% or more is placed in a pressure vessel and pressurized with pressurized gas to make the open cell ratio 100%. - By covering the container with a plastic laminate film and reducing the internal pressure, the internal pressure can uniformly reach a predetermined pressure in a short time, ensuring productivity during mass production. (b) In addition, since the foam is formed by pressurizing it in a pressure vessel, it is easy to break the walls of closed cells, and it is easy to apply pressure, so it is easy to obtain an open cell ratio of 100%. Since bubbles are broken only by pressure, there is no need to use moisture or alkali to separate the bubbles from drying at high temperatures. In other words, if the foam is kept at a high temperature, the internal pressure of the closed container may increase due to changes over time, but since pressure is only being applied, even if the foam is dried, it will only take a short time. It's okay. (c) Since there are no closed cells that contain gas, even if the insulation is left unused for a long period of time, there will be no gas diffusion from the closed cells and no pressure increase will occur.Therefore, the insulation performance of the insulation is This ensures quality stability without deterioration.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例における硬質ウレタ
ンフオームの斜視図、第2図は圧力容器中に配置
し、圧力処理中の圧力容器と硬質ウレタンフオー
ムの断面図、第3図は本発明の断熱体の断面図、
第4図は従来例の断熱性構造体の断面図である。 4……硬質ウレタンフオーム(発泡体)、5…
…圧力容器、6……硬質ウレタンフオーム、7…
…容器、8……断熱体。
FIG. 1 is a perspective view of a rigid urethane foam according to an embodiment of the present invention, FIG. 2 is a sectional view of the pressure vessel and the rigid urethane foam placed in a pressure vessel and being subjected to pressure treatment, and FIG. 3 is a cross-sectional view of the rigid urethane foam according to an embodiment of the present invention. Cross-sectional view of the insulation,
FIG. 4 is a sectional view of a conventional heat insulating structure. 4...Hard urethane foam (foam), 5...
...Pressure vessel, 6...Hard urethane foam, 7...
...Container, 8...Insulator.

Claims (1)

【特許請求の範囲】[Claims] 1 100%未満60%以上の連続気泡率を有する硬
質ウレタンフオームからなる発泡体を圧力容器内
で5Kg/cm2以上の圧力で加圧して発泡体の独立気
泡を破泡し、この破泡した断熱体を金属−プラス
チツクラミネートフイルムからなる容器内に収納
して内部を減圧したのち、容器を密閉してなる断
熱体の製造方法。
1 A foam made of hard urethane foam having an open cell ratio of less than 100% and 60% or more is pressurized in a pressure vessel at a pressure of 5 kg/cm 2 or more to burst the closed cells of the foam, and the foam is broken. A method for manufacturing a heat insulating body, which comprises storing the heat insulating body in a container made of a metal-plastic laminate film, reducing the pressure inside the container, and then sealing the container.
JP59277613A 1984-12-27 1984-12-27 Heat insulator Granted JPS61153481A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59277613A JPS61153481A (en) 1984-12-27 1984-12-27 Heat insulator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59277613A JPS61153481A (en) 1984-12-27 1984-12-27 Heat insulator

Publications (2)

Publication Number Publication Date
JPS61153481A JPS61153481A (en) 1986-07-12
JPH0463992B2 true JPH0463992B2 (en) 1992-10-13

Family

ID=17585856

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59277613A Granted JPS61153481A (en) 1984-12-27 1984-12-27 Heat insulator

Country Status (1)

Country Link
JP (1) JPS61153481A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0833606B2 (en) * 1986-09-19 1996-03-29 コニカ株式会社 Direct positive silver halide color photographic light-sensitive material

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS57133870A (en) * 1981-01-30 1982-08-18 Tokyo Shibaura Electric Co Heat insulating structure

Also Published As

Publication number Publication date
JPS61153481A (en) 1986-07-12

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