JPS6086191A - Polyolefin thermal energy storage material having heat-resistant resin film - Google Patents
Polyolefin thermal energy storage material having heat-resistant resin filmInfo
- Publication number
- JPS6086191A JPS6086191A JP58193940A JP19394083A JPS6086191A JP S6086191 A JPS6086191 A JP S6086191A JP 58193940 A JP58193940 A JP 58193940A JP 19394083 A JP19394083 A JP 19394083A JP S6086191 A JPS6086191 A JP S6086191A
- Authority
- JP
- Japan
- Prior art keywords
- heat
- heat storage
- polyolefin
- resistant resin
- resin film
- 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.)
- Granted
Links
- 229920000098 polyolefin Polymers 0.000 title claims abstract description 27
- 229920006015 heat resistant resin Polymers 0.000 title claims abstract description 8
- 239000011232 storage material Substances 0.000 title abstract description 10
- 238000004146 energy storage Methods 0.000 title abstract 3
- -1 polyethylene Polymers 0.000 claims abstract description 34
- 229920001577 copolymer Polymers 0.000 claims abstract description 13
- 150000001412 amines Chemical class 0.000 claims abstract description 7
- 238000005338 heat storage Methods 0.000 claims description 49
- 239000004698 Polyethylene Substances 0.000 abstract description 19
- 238000000034 method Methods 0.000 abstract description 19
- 229920000573 polyethylene Polymers 0.000 abstract description 19
- 230000008018 melting Effects 0.000 abstract description 11
- 238000002844 melting Methods 0.000 abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 11
- 238000004132 cross linking Methods 0.000 abstract description 8
- 239000004743 Polypropylene Substances 0.000 abstract description 5
- 239000011248 coating agent Substances 0.000 abstract description 5
- 238000000576 coating method Methods 0.000 abstract description 5
- 229920001155 polypropylene Polymers 0.000 abstract description 5
- 229920002050 silicone resin Polymers 0.000 abstract description 5
- 229930003836 cresol Natural products 0.000 abstract description 4
- 150000002989 phenols Chemical class 0.000 abstract description 3
- 230000005855 radiation Effects 0.000 abstract description 3
- GEYOCULIXLDCMW-UHFFFAOYSA-N 1,2-phenylenediamine Chemical compound NC1=CC=CC=C1N GEYOCULIXLDCMW-UHFFFAOYSA-N 0.000 abstract description 2
- QTWJRLJHJPIABL-UHFFFAOYSA-N 2-methylphenol;3-methylphenol;4-methylphenol Chemical compound CC1=CC=C(O)C=C1.CC1=CC=CC(O)=C1.CC1=CC=CC=C1O QTWJRLJHJPIABL-UHFFFAOYSA-N 0.000 abstract description 2
- 239000004642 Polyimide Substances 0.000 abstract description 2
- 239000007769 metal material Substances 0.000 abstract description 2
- 229920001721 polyimide Polymers 0.000 abstract description 2
- 229920000915 polyvinyl chloride Polymers 0.000 abstract description 2
- 239000004800 polyvinyl chloride Substances 0.000 abstract description 2
- 238000000465 moulding Methods 0.000 abstract 1
- 231100000252 nontoxic Toxicity 0.000 abstract 1
- 230000003000 nontoxic effect Effects 0.000 abstract 1
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 24
- 230000004927 fusion Effects 0.000 description 12
- 239000000126 substance Substances 0.000 description 12
- 238000011282 treatment Methods 0.000 description 8
- 230000006866 deterioration Effects 0.000 description 6
- 239000010408 film Substances 0.000 description 6
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 6
- 239000004810 polytetrafluoroethylene Substances 0.000 description 6
- 238000005054 agglomeration Methods 0.000 description 5
- 230000002776 aggregation Effects 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- 230000005865 ionizing radiation Effects 0.000 description 4
- 239000008188 pellet Substances 0.000 description 4
- 229920000642 polymer Polymers 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 230000001678 irradiating effect Effects 0.000 description 3
- 230000007774 longterm Effects 0.000 description 3
- 239000010446 mirabilite Substances 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- 238000005191 phase separation Methods 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 239000010409 thin film Substances 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- GUTLYIVDDKVIGB-OUBTZVSYSA-N Cobalt-60 Chemical compound [60Co] GUTLYIVDDKVIGB-OUBTZVSYSA-N 0.000 description 2
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N Hydroquinone Chemical compound OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 description 2
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- RDOXTESZEPMUJZ-UHFFFAOYSA-N anisole Chemical compound COC1=CC=CC=C1 RDOXTESZEPMUJZ-UHFFFAOYSA-N 0.000 description 2
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 2
- 239000000920 calcium hydroxide Substances 0.000 description 2
- 235000011116 calcium hydroxide Nutrition 0.000 description 2
- YCIMNLLNPGFGHC-UHFFFAOYSA-N catechol Chemical compound OC1=CC=CC=C1O YCIMNLLNPGFGHC-UHFFFAOYSA-N 0.000 description 2
- 229910017052 cobalt Inorganic materials 0.000 description 2
- 239000010941 cobalt Substances 0.000 description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- RSIJVJUOQBWMIM-UHFFFAOYSA-L sodium sulfate decahydrate Chemical compound O.O.O.O.O.O.O.O.O.O.[Na+].[Na+].[O-]S([O-])(=O)=O RSIJVJUOQBWMIM-UHFFFAOYSA-L 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 238000004781 supercooling Methods 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- FEXBEKLLSUWSIM-UHFFFAOYSA-N 2-Butyl-4-methylphenol Chemical compound CCCCC1=CC(C)=CC=C1O FEXBEKLLSUWSIM-UHFFFAOYSA-N 0.000 description 1
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- XUCNUKMRBVNAPB-UHFFFAOYSA-N fluoroethene Chemical group FC=C XUCNUKMRBVNAPB-UHFFFAOYSA-N 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000010559 graft polymerization reaction Methods 0.000 description 1
- 239000010438 granite Substances 0.000 description 1
- 239000011261 inert gas Substances 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 238000010907 mechanical stirring Methods 0.000 description 1
- UZKWTJUDCOPSNM-UHFFFAOYSA-N methoxybenzene Substances CCCCOC=C UZKWTJUDCOPSNM-UHFFFAOYSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- KOOMFXGDLMRWSN-UHFFFAOYSA-N n-phenylnitrous amide Chemical compound O=NNC1=CC=CC=C1 KOOMFXGDLMRWSN-UHFFFAOYSA-N 0.000 description 1
- XKLJHFLUAHKGGU-UHFFFAOYSA-N nitrous amide Chemical compound ON=N XKLJHFLUAHKGGU-UHFFFAOYSA-N 0.000 description 1
- 230000024121 nodulation Effects 0.000 description 1
- 239000012074 organic phase Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 230000004043 responsiveness Effects 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000007751 thermal spraying Methods 0.000 description 1
- 238000004073 vulcanization Methods 0.000 description 1
Abstract
Description
【発明の詳細な説明】
本発明は、結晶性ポリオレフィンを用いた浴崗潜熱利用
型の蓄熱体に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a heat storage body using crystalline polyolefin and utilizing the latent heat of bath granite.
「蓄熱」は太陽熱や工場廃熱など、その発生量と発生時
間が不安定々熱エネルギーを、一時的に貯蔵することに
よって、任意の時間に任意の量を消費できるようにする
ための技術であり、近年のエネルギー事情を背景として
1すます重要視されている。現在までに知られている蓄
熱の原理は次のように大別される。"Thermal storage" is a technology that allows you to consume any amount of thermal energy at any time by temporarily storing thermal energy, such as solar heat or factory waste heat, whose generation amount and generation time are unstable. However, given the current energy situation, it is becoming increasingly important. The principles of heat storage known to date can be broadly classified as follows.
(1)物質の顕熱を利用する方法
(2)物質の相変化潜熱を利用する方法(3)物質の化
学反応熱を利用する方法このような蓄熱の目的に利用で
きる物質が、所謂蓄熱利料であり、例えば(1)では水
や岩石のように単位体積abの熱容量が大きな物質が、
また(3)では水酸化カルシウムのように容易に温度に
より下記のよう々可逆反応を起しかつ反応熱の大なる物
質がそれぞれ蓄熱相和として検討されてきた。(1) A method that utilizes the sensible heat of a substance. (2) A method that utilizes the phase change latent heat of a substance. (3) A method that utilizes the heat of chemical reaction of a substance. Substances that can be used for such heat storage purposes are For example, in (1), a substance with a large heat capacity per unit volume ab, such as water or rock,
In addition, in (3), substances such as calcium hydroxide that easily undergo reversible reactions depending on temperature as described below and have a large heat of reaction have been studied as heat storage compounds.
Ca(OH)2□−CaO+H2O
一方(2)のイ゛目変化潜熱を利用するタイプの蓄熱体
としては、芒硝(Na2804 ・10H−zO)やハ
イポ(Na28203 ・5 H2O)のように溶融/
凝固の際の溶融潜熱を利用した所謂溶融潜熱利用型の蓄
熱体が検討されてきた。Ca(OH)2□-CaO+H2O On the other hand, as a type of heat storage body that utilizes the second latent heat of change in (2), such as mirabilite (Na2804 ・10H-zO) and hypo (Na28203 ・5H2O)
A so-called latent heat of fusion type heat storage body that utilizes the latent heat of fusion during solidification has been studied.
しかし、芒硝やハイポなどの無機水和化合物はその大部
分が過冷却や相分離現象を起すため、蓄熱体として長期
間安定表動作を行わせること−が困難である。また金属
材料を腐食するという欠点がある。However, since most of the inorganic hydrated compounds such as Glauber's Salt and Hypo cause supercooling and phase separation phenomena, it is difficult to maintain stable operation as a heat storage material for a long period of time. It also has the disadvantage of corroding metal materials.
そこで、本発明者等はこれ等の欠点の々い溶顯潜熱利用
型の蓄熱相和について種々検討の結果、結晶性のポリオ
レフィンが過冷却や相分離が全くなく、安定な蓄熱動作
を保証しうる、基本的には無害で、金属相t1に列する
腐食性を有しない、工業有機相和のうち比軸的安価であ
る等の理由により最適の蓄熱月別となり得るとの結論に
至った。Therefore, the present inventors conducted various studies on heat storage compatibility using the latent heat of molten metal, which has many drawbacks, and found that crystalline polyolefin has no supercooling or phase separation and guarantees stable heat storage operation. We have come to the conclusion that it is basically harmless, does not have corrosive properties comparable to the metal phase t1, and is relatively inexpensive compared to industrial organic phase t1.
しかし、ポリオレフィンを蓄熱体としてそのママ使用す
ると、(イ)加熱・溶融部において粘い融液と々す、こ
れが互いに融着して団塊化するので、熱媒体の流路を塞
いだり、熱媒体との熱交換を悪化させる。(ロ)また、
溶融時の体債膨張が大であるため、蓄熱器に大きな応力
を発生させる。;などの不都合がある。However, when polyolefin is used as a heat storage material, (a) a viscous melt melts in the heating/melting zone, which fuses together and forms a lump, which may block the flow path of the heat medium or deteriorates heat exchange with the (b) Also,
Since the body bond expands greatly during melting, it generates large stress in the heat storage device. ; There are other inconveniences.
これ等の不都合を回避するために、以上の蓄熱制料を適
当な強度と所定の形状を有する小容器に充填、密封する
ことにより熱交換及び取扱いに便利な蓄熱体を構成する
とともに、以上のように構成された蓄熱体を多数個集積
して蓄熱器を形成して熱媒体(空気、水、オイルなどの
流体)との間で熱交換を行わせて蓄熱の目的を達するよ
うにしていた。芒硝、ハイポ等の蓄熱利料は熱媒体とし
ての水に可溶であり、この点からも小容器の使用が不可
避であった。In order to avoid these inconveniences, a heat storage body that is convenient for heat exchange and handling is constructed by filling and sealing the above heat storage material into a small container with appropriate strength and a predetermined shape. A heat storage device was formed by integrating a large number of heat storage bodies configured in this way, and the purpose of heat storage was achieved by exchanging heat with a heat medium (fluid such as air, water, oil, etc.). . Heat storage materials such as Glauber's Salt and Hypo are soluble in water as a heat medium, and from this point of view as well, the use of small containers was inevitable.
しかし、この場合−基の蓄熱器には非常に多数の、時と
して数万個の、蓄熱体が使用されるため、以上のように
蓄熱材料を小容器に充填、□密封する方法では小容器の
製作と蓄熱利料の充填、密封の工程に要する経費が莫大
となり、時として蓄熱利料そのものの経費よりも小容器
の製作、加工費の方が高額となることもあった。However, in this case, since a very large number of heat storage bodies, sometimes tens of thousands, are used in the heat storage device, the method of filling and sealing the heat storage material into a small container as described above is not suitable. The costs involved in manufacturing the container, filling it with the heat storage charge, and sealing it were enormous, and sometimes the cost of manufacturing and processing the small container was higher than the cost of the heat storage charge itself.
これが溶融潜熱利用型蓄熱器のコヌ1−を増大させ、そ
の広範な実用化を阻害する大きな要因となっていた。This has increased the cost of the latent heat of fusion type heat storage device and has been a major factor hindering its widespread practical use.
本発明は、上記実情に鑑み前述のように溶融潜熱型蓄熱
体として優れた性質を有する結晶性ポリオレフィンを、
高価な小容器に密封することなく、しかも流動床として
用いても固着・団塊化を起こさず、さらに長期的に使用
可能な耐久性を持った経済性の高い蓄熱体を提供するこ
とを目的とするもので、その要旨は所定形状の結晶性ポ
リオレフィンあるいはその共重合体の分子間を架橋する
とともに、それにフェノール化合物あるいはアミンを加
え、その表面を耐熱性樹脂膜で被覆するようにしたもの
である。In view of the above circumstances, the present invention provides a crystalline polyolefin having excellent properties as a molten latent heat type heat storage body as described above.
The purpose is to provide a highly economical heat storage material that does not need to be sealed in an expensive small container, does not cause sticking or clumping even when used as a fluidized bed, and is durable and can be used for a long period of time. The gist is to crosslink the molecules of crystalline polyolefin or its copolymer in a predetermined shape, add a phenol compound or amine to it, and cover the surface with a heat-resistant resin film. .
即ち、本発明は以上のように構成することにより、結晶
性ポリエチレンは加熱により溶融してもゲル状になって
流動せず、且つ適度の強度を有し、しかも溶融状態で粘
着性を示さな7くなり、さらに熱劣化を受けにくくなる
。そこで、蓄熱体とする゛のに高価な小容器を必要とせ
ず、また、流動床として用いる場合にも固着・団塊化を
起こさず、さらに長期使用可能な耐久性を持ち、本発明
の所期の目的を達成することができたのである。That is, by configuring the present invention as described above, crystalline polyethylene becomes gel-like and does not flow even when melted by heating, has appropriate strength, and does not exhibit stickiness in the molten state. 7, making it even less susceptible to thermal deterioration. Therefore, the purpose of the present invention is to eliminate the need for an expensive small container when used as a heat storage body, to prevent sticking or clumping when used as a fluidized bed, and to have durability for long-term use. We were able to achieve this goal.
更に、本発明によればポリオレフィンの溶融時の体積膨
張率が減少するため、これを収容する蓄熱器に加熱時に
大きガ応力を発生させることもない。Further, according to the present invention, since the volumetric expansion coefficient of the polyolefin when melted is reduced, large stress is not generated in the heat storage device housing the polyolefin during heating.
ここで、(1)結晶性ポリオレフィンあるいはその共重
合体の分子間の架橋、(2)フェノール化合物あるいは
アミンの添加、(3)耐熱性樹脂膜による被覆の三つの
処理のうち、もし、(1)の処理が欠けた場合には蓄熱
体は加熱・融解時に相互に固着・団塊化し、(2)の処
理が欠けた場合には長期間使用すると熱劣化により溶融
潜熱量が減少し、最後には熱を蓄えることができなくな
る。Here, among the three treatments of (1) intermolecular crosslinking of crystalline polyolefin or its copolymer, (2) addition of a phenol compound or amine, and (3) coating with a heat-resistant resin film, if (1 If the treatment in (2) is missing, the heat storage bodies will stick to each other and become lumps when heated and melted, and if the treatment in (2) is missing, the amount of latent heat of fusion will decrease due to thermal deterioration after long-term use, and finally cannot store heat.
また、(3)の処理が欠けた場合には、流動床として用
いる際に高温で溶融した状態の蓄熱体表面がいくらか粘
着性を示すため、蓄熱体同志が固着・団塊化を起こして
再度使用できなくなるという不都合を生ずる。したがっ
て、以上三つの処理は本発明の目的のために必要不可欠
である。In addition, if the treatment in (3) is not completed, the surface of the heat storage body that is molten at high temperature will exhibit some stickiness when used as a fluidized bed, causing the heat storage bodies to stick to each other and form lumps before being used again. This causes the inconvenience of not being able to do so. Therefore, the above three processes are essential for the purpose of the present invention.
これら三つの処理は任意の順番で行うことができる。These three processes can be performed in any order.
、本発明では蓄熱材料として結晶性ポリエチレンや結晶
性ポリプロピレンなどの結晶性ポリオレフィンあるいは
その共重合体、特に高結晶性ポリオレフィンあるいはそ
の共重合体’&M状、棒状体、板状体、円管状体などの
所定形状に成形したものを使用する。なお、これら成形
体はその直径(または厚み)を2〜8闘にとることによ
り、満足すべき熱応答性を持つ蓄熱器を一般に構成する
ことができる。In the present invention, a crystalline polyolefin such as crystalline polyethylene or crystalline polypropylene or a copolymer thereof, particularly a highly crystalline polyolefin or a copolymer thereof, is used as a heat storage material. Use a product that has been molded into a predetermined shape. In addition, by setting the diameter (or thickness) of these molded bodies to 2 to 8 mm, a heat storage device having satisfactory thermal responsiveness can generally be constructed.
また、本発明において結晶性ポリオレフィンあるいはそ
の共重合体の分子間を架橋させる方法として、放射線法
、水架橋法、イオン架橋法、過酸化物法、加硫法などが
挙げられる。Further, in the present invention, methods for crosslinking the molecules of the crystalline polyolefin or its copolymer include a radiation method, a water crosslinking method, an ionic crosslinking method, a peroxide method, a vulcanization method, and the like.
このうち、放射線法において使用される電離性放射線と
してはコバルト600ガンマ線が好適であるが、これに
限定されず〒E子線や短波長X線など、所謂電離性放射
線は全て使用できる。Among these, cobalt-600 gamma rays are preferred as the ionizing radiation used in the radiation method, but the present invention is not limited to this, and all so-called ionizing radiations such as E-son rays and short wavelength X-rays can be used.
電離性放射線の照射線量は、105〜108ラドであり
、それ以下であると融着や団塊化が起こり、それ以上で
あるとポリオレフィンの溶融熱が減少し、蓄熱密度が小
さくなるので、好ましくない。The irradiation dose of ionizing radiation is 105 to 108 rad, and if it is less than that, fusion and agglomeration will occur, and if it is more than that, the heat of fusion of the polyolefin will decrease and the heat storage density will become small, which is not preferable. .
また電離性放射線を照射するときの雰囲気は真空或は不
活性ガス中で行うのが好ましい。Further, it is preferable that the atmosphere for irradiating the ionizing radiation is a vacuum or an inert gas.
本発明に用いられるフェノール化合物あるいはアミンと
しては、フェノール、クレゾール、ヒドロキノン、カテ
コール、アニソール、キンレノ−/L/、N−ニトロソ
アニリン、N−ニトロソアミン、フェニレンジアミン、
エチレンジアミン及びそれらの物質の誘導体などが挙げ
られる。これらの物質は単独で用いてもよいし、2種以
上混合して用いてもよい。Phenol compounds or amines used in the present invention include phenol, cresol, hydroquinone, catechol, anisole, quinreno-/L/, N-nitrosoaniline, N-nitrosamine, phenylenediamine,
Examples include ethylenediamine and derivatives of these substances. These substances may be used alone or in combination of two or more.
これらの物質は例えば次のような処理によってポリオレ
フィンあるいはその共重合体に添加される。1ず、ポリ
オレフィンあるいはその共重合体をその融点上10〜2
0℃に加熱して融解し、その融液にこれらの物質あるい
はその粉末を加え、機械的に攪拌を行って混合する。あ
るいは、加熱して柔らかくなったポリオレフィンあるい
はその共重合体にこれらの物質あるいはその微粉末を混
和し、機械的撹拌を行って表面に付着させる。また、こ
れらの物質の溶液にポリオレフィンあるいはその共重合
体を浸漬し、しばらく放置した後、乾燥して溶媒を除去
するなどの方法もある。These substances are added to polyolefins or copolymers thereof by, for example, the following treatment. 1. Polyolefin or its copolymer has a melting point of 10 to 2
The substance or its powder is added to the melt by heating to 0° C. and mixed by mechanical stirring. Alternatively, these substances or fine powder thereof are mixed with polyolefin or its copolymer which has been softened by heating, and mechanically stirred to adhere to the surface. Another method is to immerse polyolefin or its copolymer in a solution of these substances, leave it for a while, and then dry it to remove the solvent.
フェノ−tv化合物あるいはアミンのポリオレフィンあ
るいはその共重合体に71する添加量は通常、数重量%
で良いが、蓄熱体の使用期間により、それが長い場合は
添加量を増やすなど、適宜増減することができる。The amount of the pheno-tv compound or amine added to the polyolefin or copolymer thereof is usually several percent by weight.
However, depending on the usage period of the heat storage body, if the period is long, the amount added can be increased or decreased as appropriate.
更に本発明において用いられる耐熱性樹脂としては、フ
ッ素樹脂、シリコン樹脂、ポリ塩化ビニール、ポリプロ
ピレンあるいはポリイミドなどが挙げられる。Furthermore, examples of the heat-resistant resin used in the present invention include fluororesin, silicone resin, polyvinyl chloride, polypropylene, and polyimide.
これらの樹脂膜で表面を被覆する方法としては、ポリマ
ー粉末の溶融、ポリマーエマルションへの浸漬・乾燥、
ペーストレシンによる塗布、ポリマー溶液の吹き付け、
焼き伺け、糊引き、ポリマー粉末の溶射、表面へのグラ
フト重合々とが挙げられる。Methods for coating surfaces with these resin films include melting polymer powder, dipping in polymer emulsion and drying,
Application with paste resin, spraying with polymer solution,
Examples include baking, sizing, thermal spraying of polymer powder, and graft polymerization on the surface.
こうして得られた蓄熱体は、蓄熱密度が大きく、湯冷や
相分離を起こさず、溶融時において融着・団塊化を起こ
さない。しかも、溶融時における体積膨張率が大幅に低
下し、長期間の使用に際しても蓄熱能力が低下しないの
で、安定な蓄熱動作が可能である。The heat storage body thus obtained has a high heat storage density, does not undergo hot water cooling or phase separation, and does not cause fusion or agglomeration during melting. Moreover, the coefficient of volumetric expansion during melting is significantly reduced, and the heat storage capacity does not decrease even during long-term use, so stable heat storage operation is possible.
本発明による蓄熱体は以上のように安価・経済的な方法
で融着・団塊化及び熱劣化を防止したもので、太陽エネ
ルギーや工場廃熱などの低温熱エネルギーの回収・利用
に好適なものである。As described above, the heat storage body of the present invention prevents fusion, agglomeration, and thermal deterioration using a cheap and economical method, and is suitable for recovering and utilizing low-temperature thermal energy such as solar energy and factory waste heat. It is.
次に実施例によって本発明をさらに詳細に説明する。Next, the present invention will be explained in more detail with reference to Examples.
実施例
第1図のよう々蓄熱試験装置を製作し、その中に充填す
べき、蓄熱体1について、後述するような種々の方法で
団塊化及び熱劣化防止のための処理を行った。第1図に
おいて、2は断熱相開層、3は鋼板製容器、4は多孔板
、5は電気ヒータ、6は空気ポンプである。6から送入
される空気を5で加熱し、その温度を熱電対7および温
度メータ8で監視しつつ、蓄熱体1の層に吹込んでこれ
を昇温させる。このとき、吹込点空気の温度をポリオレ
フィンの融点上15〜25℃となるように一定とすると
、ポリオレフィンは溶融を起し、その融解熱に4′目当
する一I:;:不ルキをポリオレフィン内部に県債する
ことに。EXAMPLE A heat storage test apparatus was manufactured as shown in FIG. 1, and the heat storage bodies 1 to be filled therein were treated to prevent agglomeration and thermal deterioration by various methods as described below. In FIG. 1, 2 is an adiabatic phase open layer, 3 is a steel plate container, 4 is a perforated plate, 5 is an electric heater, and 6 is an air pump. Air introduced from 6 is heated at 5, and while its temperature is monitored by a thermocouple 7 and a temperature meter 8, it is blown into the layer of the heat storage body 1 to raise its temperature. At this time, if the temperature of the air at the blowing point is kept constant at 15 to 25 degrees Celsius above the melting point of the polyolefin, the polyolefin will melt, and the heat of fusion will cause the polyolefin to I decided to make prefectural bonds internally.
々る。That's it.
次に、電気ヒータ5の出力を調節して、吹込゛み空気の
温度を、ポリオレフィンの融点より15〜25℃下方に
なるようにすると、ポリオレフィンはその融解熱を放出
しつつ凝固を起し、この間、その融点に4目当する一定
温度の空気が第1図の試験装置の出口9に得られること
になる。Next, when the output of the electric heater 5 is adjusted so that the temperature of the blown air is 15 to 25 degrees Celsius below the melting point of the polyolefin, the polyolefin solidifies while releasing its heat of fusion. During this time, air at a constant temperature corresponding to its melting point will be available at the outlet 9 of the test apparatus in FIG.
このとき用いられたポリオレフィンは商品名5hole
x F 6050 C1直径約3mmのポリエチレンベ
レットである。このような蓄熱体が溶融・団
凝固の繰り返しにより、4間塊化を起すと、蓄熱体の層
の中の空気流路がせばめられ、効率的な蓄熱体/空気間
の熱交換が不用化となるため、非常な不都合を生ずる。The polyolefin used at this time was under the trade name 5hole.
x F 6050 C1 A polyethylene pellet with a diameter of approximately 3 mm. When such a heat storage body becomes agglomerated due to repeated melting and solidification, the air flow path in the layer of the heat storage body becomes narrower, making efficient heat exchange between the heat storage body and air unnecessary. This causes great inconvenience.
そこで、団塊化防止及び熱劣化防止を目的に、次に述べ
るような処理を行って試料を準備した。Therefore, for the purpose of preventing agglomeration and thermal deterioration, samples were prepared by performing the following treatment.
(1) ポリエチレンに107ラドのコバルト6oガン
マ線を照射した後、水を加えたポリテトラフルオロエチ
レン串デイヌバージョン液にひたし、よく振って分散さ
せてから、102℃の空気恒温槽中で水分を蒸発・除去
し、ポリエチレンの表面をポリテトラフルオロエチレン
薄膜で被覆した。これを2,6シー(、−ブチルフレソ
ールの10重fj1%のベンセン溶液中に2屓夜浸漬し
た後、ベンセンで軽く洗浄し、空気中で乾燥した。(1) After irradiating polyethylene with 107 rad of cobalt 6o gamma rays, soak it in a polytetrafluoroethylene skewer solution containing water, shake well to disperse, and then remove the moisture in an air thermostat at 102°C. After evaporation and removal, the surface of the polyethylene was coated with a polytetrafluoroethylene thin film. This was immersed for 2 nights in a 1% benzene solution of 2,6 C(-butyl fresol), washed lightly with benzene, and dried in the air.
(2) ポリエチレンを水架橋した後、シリコン樹脂モ
ノマーを20重量%溶解した溶剤中にひたし、よく振っ
て分散させてから適量の触媒を加え、115℃の空気恒
温槽中で全体を振とうさせながら、溶剤を蒸発・除去す
るとともに、シリコン樹脂を重合させ、ポリエチレンベ
レットの表面をシリコン樹脂の薄膜で被覆シタ。これe
N−フェニル−N′−シクロへキシル−イド−フェニレ
ンジアミンの15重量%のベンゼン溶液で(1)と同様
に処理した。(2) After crosslinking polyethylene with water, soak it in a solvent containing 20% by weight of silicone resin monomer, shake well to disperse it, add an appropriate amount of catalyst, and shake the whole thing in an air constant temperature bath at 115°C. While the solvent is being evaporated and removed, the silicone resin is polymerized and the surface of the polyethylene pellet is coated with a thin film of silicone resin. This e
It was treated in the same manner as in (1) with a 15% by weight benzene solution of N-phenyl-N'-cyclohexyl-ido-phenylenediamine.
(3) ポリエチレンに5X107ラドのコバルト6d
ガンマ線を照射しながらアルゴンガスにより塩化ビニー
ル蒸気を送り込んで、ポリエチレンと塩化ビニ−)vf
共存させ、ポリエチレンの表面に塩化ビニールをグラフ
ト重合させ、被覆せしめた。これを2,2′−メチレン
ービヌ(4−メチル−6−L−ブチルフェノールの10
重量%のベンゼン溶液で(1)と同様に処理した。(3) 5x107 rad cobalt 6d on polyethylene
While irradiating with gamma rays, vinyl chloride vapor is sent in using argon gas to remove polyethylene and vinyl chloride (vf).
The surface of polyethylene was graft-polymerized and coated with vinyl chloride. 2,2'-methylene-vinu(4-methyl-6-L-butylphenol)
It was treated in the same manner as in (1) with a wt % benzene solution.
(4)ポリエチレンを加熱してt,4111解し、その
中に、5重量%のN 、 N’−ジフェニル−)−フェ
ー・二゛
レンジアミンを加えて投拌し、溶解さぜた。;1これを
直径3 mmの球状に成形し、室1jRr iで肌冷し
た後、3×107ラドのコバルト60のガンマ線で照射
した。その後、(1)と同様にしてポリテトラフルオロ
エチレン簿膜で表面被覆した。(4) Polyethylene was heated to dissolve t,4111, and 5% by weight of N,N'-diphenyl-)-phenylene diamine was added and stirred to dissolve. ;1 This was formed into a spherical shape with a diameter of 3 mm, cooled in a chamber 1jRri, and then irradiated with cobalt-60 gamma rays of 3×10 7 rad. Thereafter, the surface was coated with a polytetrafluoroethylene film in the same manner as in (1).
以上のごとき種々の処理をイJっだ蓄熱体ベレットを第
1図に示した試験装置内に装入し、既に説明を加えたよ
うな加熱と冷却を杓って、ポリエチレンの溶融と凝固を
1日1回ずつ、6力月にわたって繰り返したのち、これ
を外部に取り出して、その団塊化の状況を観,察し、溶
融潜熱量を測定した。その結果、これら(1)〜(4)
の試料はほとんど固着を起こしておらず、容易に個々の
ベレット粒子が分離してばらばらに々す、溶融潜熱量も
ほとんど変化しなかった。The heat storage pellet that has been subjected to the various treatments described above is placed in the test equipment shown in Figure 1, and heated and cooled as already explained to melt and solidify the polyethylene. After repeating this process once a day for 6 months, it was taken out to observe and observe the state of nodule formation, and the latent heat of fusion was measured. As a result, these (1) to (4)
The sample showed almost no sticking, the individual pellet particles easily separated and scattered, and the latent heat of fusion hardly changed.
比較例
次のよう々処理を行った試料を用いて第1図に示した試
l@装置によって実7jfti例と同様にして6力月間
の試験を行った。Comparative Example A 6-month test was conducted in the same manner as in the actual example using the test equipment shown in FIG. 1 using samples treated as follows.
(1)ポリエチレンに107ラドのコバルト60ガンマ
線を照射した。(1) Polyethylene was irradiated with 107 rad of cobalt-60 gamma rays.
(2) (1)の処理を行ったポリエチレンを、水を加
えたポリテトラフルオロエチレン・テイヌバーション液
にひたし、よく振って分散させてから、102℃の空気
恒温槽中で水分を蒸発・除去し、ポリエチレンの表面を
ポリテトラフルオロエチレン薄膜で被覆した。(2) The polyethylene treated in (1) is soaked in a polytetrafluoroethylene teinubation solution containing water, shaken well to disperse it, and then evaporated in an air constant temperature bath at 102°C. The surface of the polyethylene was then coated with a polytetrafluoroethylene thin film.
(3) (1)の処理を行ったポリエチレンを2.6
ジーも一ブチルクレゾールの10重量%のベンゼン溶液
中に2属夜浸漬した後、ベンゼンで軽く洗浄し、空気中
で乾燥し/ζ。(3) 2.6% of the polyethylene treated in (1)
The mixture was soaked overnight in a 10% by weight solution of monobutyl cresol in benzene, then washed lightly with benzene and dried in air/ζ.
(4)ポリエチレンを、水を加えたポリテトラフルオロ
エチレン・デイヌパーション液にひたし、よく振って分
散してから102℃の空気恒温槽中で水分を蒸発・除去
し、ポリエチレンの表面をポリテトラフルオロエチレン
薄膜で被覆した。これを2,6シーも一ブチルクレゾー
ルの10重量%のベンゼン溶液中に2凪夜浸漬した後、
ベンゼンで軽く洗浄し、空気中で乾燥した。(4) Soak polyethylene in polytetrafluoroethylene Daynepersion solution with water added, shake well to disperse, and then evaporate and remove water in an air constant temperature bath at 102°C. It was coated with a thin fluoroethylene film. After immersing this in a 10% by weight benzene solution of monobutyl cresol for 2.6 nights,
Washed briefly with benzene and dried in air.
この結果を1とめると次表のようで4うった。If we take this result as 1, we get 4 as shown in the following table.
以上のように、(1)分子間架橋、(2)フェノール化
合物あるいはアミンの添加、(3)鍾耐熱性樹u4膜に
よる被覆の三つの処理のうち、一つでも徒けると固着、
団塊化あるいは熱劣化により、埠4期間の使用が不可能
であった。As mentioned above, if any one of the three treatments (1) intermolecular crosslinking, (2) addition of a phenol compound or amine, and (3) coating with a heat-resistant resin U4 film fails, it will stick.
Due to compaction or thermal deterioration, the wharf could not be used for the 4th period.
第1図は本発明の一実施例である蓄熱器の断面図である
。
図中、1は蓄熱体、2は断熱材、3は鋼板製容器、4は
多孔板、5は″fL気ヒータ、6は空気ポンプ、7は熱
−4対、8は温度メータ、9は出口、である。FIG. 1 is a sectional view of a heat storage device according to an embodiment of the present invention. In the figure, 1 is a heat storage body, 2 is a heat insulator, 3 is a steel plate container, 4 is a perforated plate, 5 is a "fL air heater, 6 is an air pump, 7 is a heat-4 pair, 8 is a temperature meter, and 9 is a It's the exit.
Claims (1)
の分子間を架橋するとともに、それにフェノール化合物
あるいはアミンを加え、その表面を耐熱性樹脂膜で被范
するようにしたことを特徴とする蓄熱体。A heat storage body characterized in that the molecules of a crystalline polyolefin or a copolymer thereof in a predetermined shape are crosslinked, a phenol compound or an amine is added thereto, and the surface thereof is covered with a heat-resistant resin film.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58193940A JPS6086191A (en) | 1983-10-17 | 1983-10-17 | Polyolefin thermal energy storage material having heat-resistant resin film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58193940A JPS6086191A (en) | 1983-10-17 | 1983-10-17 | Polyolefin thermal energy storage material having heat-resistant resin film |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6086191A true JPS6086191A (en) | 1985-05-15 |
| JPS6341958B2 JPS6341958B2 (en) | 1988-08-19 |
Family
ID=16316269
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58193940A Granted JPS6086191A (en) | 1983-10-17 | 1983-10-17 | Polyolefin thermal energy storage material having heat-resistant resin film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6086191A (en) |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4711813A (en) * | 1985-11-22 | 1987-12-08 | University Of Dayton | Polyethylene composites containing a phase change material having a C14 straight chain hydrocarbon |
| US4908166A (en) * | 1985-11-22 | 1990-03-13 | University Of Dayton | Method for preparing polyolefin composites containing a phase change material |
| US5053446A (en) * | 1985-11-22 | 1991-10-01 | University Of Dayton | Polyolefin composites containing a phase change material |
| US5106520A (en) * | 1985-11-22 | 1992-04-21 | The University Of Dayton | Dry powder mixes comprising phase change materials |
| JPH04270778A (en) * | 1991-02-26 | 1992-09-28 | Sekisui Plastics Co Ltd | Latent-heat type heat-accumulation material and its production |
| US5211949A (en) * | 1990-01-09 | 1993-05-18 | University Of Dayton | Dry powder mixes comprising phase change materials |
| US5254380A (en) * | 1985-11-22 | 1993-10-19 | University Of Dayton | Dry powder mixes comprising phase change materials |
| WO1995018847A1 (en) * | 1994-01-07 | 1995-07-13 | Schuetz Wilhelm | Latent heat storage media |
| US5477917A (en) * | 1990-01-09 | 1995-12-26 | The University Of Dayton | Dry powder mixes comprising phase change materials |
| US6652771B2 (en) | 2001-07-11 | 2003-11-25 | Ronald M. Carn | Phase change material blend, method for making, and devices using same |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH01318451A (en) * | 1988-06-20 | 1989-12-22 | Fujitsu General Ltd | Teleconference network system |
-
1983
- 1983-10-17 JP JP58193940A patent/JPS6086191A/en active Granted
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4711813A (en) * | 1985-11-22 | 1987-12-08 | University Of Dayton | Polyethylene composites containing a phase change material having a C14 straight chain hydrocarbon |
| US4908166A (en) * | 1985-11-22 | 1990-03-13 | University Of Dayton | Method for preparing polyolefin composites containing a phase change material |
| US5053446A (en) * | 1985-11-22 | 1991-10-01 | University Of Dayton | Polyolefin composites containing a phase change material |
| US5106520A (en) * | 1985-11-22 | 1992-04-21 | The University Of Dayton | Dry powder mixes comprising phase change materials |
| US5254380A (en) * | 1985-11-22 | 1993-10-19 | University Of Dayton | Dry powder mixes comprising phase change materials |
| US5211949A (en) * | 1990-01-09 | 1993-05-18 | University Of Dayton | Dry powder mixes comprising phase change materials |
| US5477917A (en) * | 1990-01-09 | 1995-12-26 | The University Of Dayton | Dry powder mixes comprising phase change materials |
| JPH04270778A (en) * | 1991-02-26 | 1992-09-28 | Sekisui Plastics Co Ltd | Latent-heat type heat-accumulation material and its production |
| WO1995018847A1 (en) * | 1994-01-07 | 1995-07-13 | Schuetz Wilhelm | Latent heat storage media |
| US6652771B2 (en) | 2001-07-11 | 2003-11-25 | Ronald M. Carn | Phase change material blend, method for making, and devices using same |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6341958B2 (en) | 1988-08-19 |
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