JP2002030280A - Method for producing granule of agent for preventing supercooling of salt hydrate - Google Patents

Method for producing granule of agent for preventing supercooling of salt hydrate

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Publication number
JP2002030280A
JP2002030280A JP2000213916A JP2000213916A JP2002030280A JP 2002030280 A JP2002030280 A JP 2002030280A JP 2000213916 A JP2000213916 A JP 2000213916A JP 2000213916 A JP2000213916 A JP 2000213916A JP 2002030280 A JP2002030280 A JP 2002030280A
Authority
JP
Japan
Prior art keywords
salt hydrate
supercooling
melt
mixture
heat storage
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.)
Pending
Application number
JP2000213916A
Other languages
Japanese (ja)
Inventor
Kenji Saida
健二 才田
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.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo Chemical Co 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 Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP2000213916A priority Critical patent/JP2002030280A/en
Publication of JP2002030280A publication Critical patent/JP2002030280A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide an economical, safe and simple method suitable for mass- production for producing an agent for preventing supercooling, comprising a salt hydrate. SOLUTION: This method for producing the granule of the agent for preventing supercooling, comprising the salt hydrate is characterized in that a mixture of a molten liquid of the salt hydrate kept at a temperature not less than the melting point with a supporting crystal for preventing the supercooling is kept at the temperature not less than the melting point to form droplets on a water-repellent material, and cooling and solidifying the resultant mixture. The heat storage material or the heat storage device is obtained by using the granules of the agent for preventing the supercooling of the salt hydrate, produced by the production method.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は塩水和物の過冷却防
止剤の製造方法に関する。さらに詳しくは、本発明は潜
熱蓄熱材に好適に用いられる塩水和物の過冷却防止剤顆
粒の製造方法に関する。
[0001] The present invention relates to a method for producing a supercooling inhibitor for salt hydrate. More specifically, the present invention relates to a method for producing a salt hydrate supercooling inhibitor granule suitably used for a latent heat storage material.

【0002】[0002]

【従来の技術】固液相変化の性質を有する塩水和物を蓄
熱材料として利用しようとする提案が数多くなされてお
り、既に、床暖房等の分野において実用化されている。
代表的な塩水和物としては、硫酸ナトリウム10水塩、
塩化カルシウム6水塩、リン酸水素二ナトリウム12水
塩、酢酸ナトリウム3水塩等がある。これらの塩水和物
はいずれも、それ単独では過冷却現象を呈し、それが蓄
熱材としての利用の大きな障壁となっていた。この障壁
を克服するために過冷却防止剤又は過冷却防止方法につ
いての提案が多数なされてきた。
2. Description of the Related Art Many proposals have been made to use a salt hydrate having a property of solid-liquid phase change as a heat storage material, and it has already been put to practical use in the field of floor heating and the like.
Representative salt hydrates include sodium sulfate decahydrate,
Calcium chloride hexahydrate, disodium hydrogen phosphate dodecahydrate, sodium acetate trihydrate and the like. Each of these salt hydrates alone exhibited a supercooling phenomenon, which was a great barrier to use as a heat storage material. Many proposals have been made for a supercooling inhibitor or a method for preventing supercooling in order to overcome this barrier.

【0003】硫酸ナトリウム10水塩に対する過冷却防
止剤として四ホウ酸ナトリウム10水塩が有効であるこ
とが1952年に判明した。この組合せは同一晶系に属
し、結晶の格子定数も近いことから、ヘテロエピタキシ
ャル成長に基づく核形成であることが分かっている。こ
の発見の後、その他の塩水和物について、結晶学的アプ
ローチで探索が続けられたが、同様な組み合わせは未だ
に見い出されていない。
It was found in 1952 that sodium tetraborate decahydrate was effective as a supercooling inhibitor for sodium sulfate decahydrate. Since this combination belongs to the same crystal system and the lattice constant of the crystal is close, it is known that nucleation is based on heteroepitaxial growth. After this discovery, the search for other salt hydrates was continued with a crystallographic approach, but similar combinations have not yet been found.

【0004】一方、酢酸ナトリウム3水塩について、特
定の担持結晶を用いる方法が提案されている。担持結晶
としてはリン酸水素二ナトリウム、リン酸三ナトリウム
などのナトリウム塩(特公昭61−42957号公報、
特公平2−15598号公報)などが開示されている。
これらは酢酸ナトリウム3水塩の融液の中に担持結晶や
プレス成形した担持結晶を入れ、強制冷却することによ
って融液を固化させる操作を行う方法である。これらの
方法では、一度は融液を固化させて担持結晶の表面に酢
酸ナトリウム3水塩を固化させる工程を経なければ過冷
却防止効果が得られないので、容器に充填後に過冷却状
態を破るため強制冷却−固化させる操作が必須であり、
大量生産においては不都合な方法である。また、担持結
晶の量も多く用いる必要がある。強制冷却の代わりに種
結晶を投入して融液を固化させる方法を採用する場合に
は、該種結晶が融解しないよう、あらかじめ融液を過冷
却状態にしておく必要があり、やはり大量生産には不都
合な方法である。
On the other hand, a method using a specific supported crystal for sodium acetate trihydrate has been proposed. As the supported crystals, sodium salts such as disodium hydrogen phosphate and trisodium phosphate (JP-B-61-42957,
JP-B-2-15598) and the like are disclosed.
In these methods, a supported crystal or a press-formed supported crystal is placed in a melt of sodium acetate trihydrate, and the melt is solidified by forced cooling. In these methods, the supercooling prevention effect cannot be obtained unless the melt is solidified once to solidify sodium acetate trihydrate on the surface of the supported crystal, so that the supercooled state is broken after filling the container. Therefore, forced cooling-solidification operation is essential,
This is an inconvenient method for mass production. In addition, it is necessary to use a large amount of supported crystals. When adopting a method of solidifying the melt by introducing a seed crystal instead of forced cooling, it is necessary to pre-cool the melt in advance so that the seed crystal does not melt. Is an inconvenient method.

【0005】これを解決する方法として、特公平1−5
1515号公報や特公昭58−27301号公報には、
融液に担持結晶(基材)としてピロリン酸ナトリウムを
入れ、これをそのまままたは取り出して冷却固化させて
別途、過冷却防止剤を製造する方法が開示されている。
特開昭64−75583号公報には、融液に担持結晶を
入れ、これを一度固化させたのち再び加熱融解し、その
後融液から濾取した結晶を過冷却防止に用いる方法が開
示されている。これらの方法においては、充填用の融液
に過冷却防止剤を添加すればよいので、操作性は改善さ
れるが、過冷却防止剤を製造するために融液を調製する
ことが必要であり、また融液から濾取したあと固化する
ので、過冷却防止剤として使用するには粉砕をする必要
があるなどのため、エネルギー消費量、操作安全性、操
作簡便性などにおいて問題点がある。更に、本発明者ら
は特開平10−298543号公報において、塩水和物
と過冷却防止用担持結晶とを混合摩砕する塩水和物の過
冷却防止剤の製造方法を開示した。この方法は、融液を
調製する必要がないという利点があるが、混合摩砕で
は、1バッチ当りの処理量が少ないため多くのバッチ数
が必要となること、混合摩砕によって得られる粉末を過
冷却防止剤として使用するには少量ずつ包装するか成形
するかあるいは粉体供給機で粉末のまま添加するかなど
の方策を講じなければならないという問題点があった。
As a method for solving this, Japanese Patent Publication No. 1-5
No. 1515 and Japanese Patent Publication No. 58-27301,
There is disclosed a method of separately adding a supercooling inhibitor by adding sodium pyrophosphate as a supporting crystal (base material) to a melt and solidifying it by cooling as it is or by taking out the sodium pyrophosphate.
Japanese Patent Application Laid-Open No. 64-75583 discloses a method in which a supported crystal is put into a melt, solidified once, heated and melted again, and then the crystal filtered from the melt is used to prevent supercooling. I have. In these methods, operability is improved because a supercooling inhibitor may be added to the filling melt, but it is necessary to prepare the melt to produce the supercooling inhibitor. Further, since it is solidified after being filtered off from the melt, it needs to be crushed to be used as a supercooling inhibitor, and thus has problems in energy consumption, operation safety, operability and the like. Furthermore, the present inventors have disclosed in JP-A-10-298543 a method for producing a salt hydrate supercooling inhibitor by mixing and grinding a salt hydrate and a supercooling-preventing supporting crystal. This method has the advantage that it is not necessary to prepare a melt.However, in the case of mixing and milling, a large number of batches are required because the throughput per batch is small. In order to use it as a supercooling inhibitor, there is a problem in that it is necessary to take measures such as packaging or molding a small amount at a time, or adding the powder as it is in a powder feeder.

【0006】[0006]

【発明が解決しようとする課題】本発明の目的は、塩水
和物の過冷却防止剤の製造方法において、より経済的で
より安全・簡便な、大量生産に好都合な方法を提供する
ことにある。
SUMMARY OF THE INVENTION An object of the present invention is to provide a more economical, safer and simpler method for producing supercooling inhibitors for salt hydrates, which is convenient for mass production. .

【0007】[0007]

【課題を解決するための手段】本発明者らは、かかる状
況下に鋭意検討を行った結果、塩水和物の融液と過冷却
防止用担持結晶との混合物の液滴を形成後、冷却して顆
粒状にすることにより、上記課題を解決できることを見
出し、本発明を完成させるに至った。
Means for Solving the Problems The present inventors have conducted intensive studies in such a situation, and as a result, formed droplets of a mixture of a melt of a salt hydrate and a supporting crystal for preventing supercooling, and then cooled the mixture. It has been found that the above-mentioned problems can be solved by making the particles into a granular form, and the present invention has been completed.

【0008】すなわち、本発明は、融点以上に保持され
た塩水和物の融液と過冷却防止用担持結晶との混合物を
融点以上に保持して揆水性材料の上に液滴を形成、該
混合物を冷却固化させることを特徴とする塩水和物の過
冷却防止剤顆粒の製造方法、及びその製造方法にて製造
される塩水和物の過冷却防止剤顆粒用いる蓄熱材又は蓄
熱装置に関するものである。
Namely, the present invention is, after forming the droplet on the揆水material mixture is held above the melting point of the melt and the supercooling-preventing supported crystalline salt hydrates held above its melting point, A method for producing a superhydrate inhibitor granule of a salt hydrate characterized by cooling and solidifying the mixture, and a heat storage material or a heat storage device using the supercool inhibitor granule of a salt hydrate produced by the method. It is.

【0009】[0009]

【発明の実施の形態】以下にこれらの発明について詳し
く説明する。本発明において塩水和物は、固液相変化の
性質を有する塩水和物であって、例えば蓄熱材として利
用されるものである。代表的な塩水和物としては、硫酸
ナトリウム10水塩、塩化カルシウム6水塩、リン酸水
素二ナトリウム12水塩、リン酸水素二ナトリウム7水
塩、硝酸カルシウム4水塩、酢酸ナトリウム3水塩、塩
化ストロンチウム6水塩などがある。これらは単独ある
いは共晶塩、あるいは融点調整剤との組成物として用い
られる。また結晶水の他に水分を小過剰添加することが
好ましい場合もある。
BEST MODE FOR CARRYING OUT THE INVENTION Hereinafter, these inventions will be described in detail. In the present invention, the salt hydrate is a salt hydrate having a property of solid-liquid phase change, and is used, for example, as a heat storage material. Representative salt hydrates include sodium sulfate decahydrate, calcium chloride hexahydrate, disodium hydrogen phosphate decahydrate, disodium hydrogen phosphate decahydrate, calcium nitrate tetrahydrate, sodium acetate trihydrate And strontium chloride hexahydrate. These are used alone or as a composition with a eutectic salt or a melting point modifier. In some cases, it is preferable to add a small excess of water in addition to the water of crystallization.

【0010】本発明において過冷却防止剤用担持結晶と
しては、塩水和物を担持し得る結晶が用いられる。例え
ば塩水和物が酢酸ナトリウム3水塩の場合は、担持結晶
としてはリン酸水素二ナトリウム、リン酸二水素一ナト
リウム、リン酸三ナトリウム、四ホウ酸ナトリウム、臭
化ナトリウム、硫酸ナトリウムおよびそれらの水和物な
どが例示される。また、塩水和物として塩化ストロンチ
ウム6水塩の場合は、担持結晶としては水酸化ストロン
チウム8水塩などが、塩水和物がリン酸水素二ナトリウ
ム12水塩の場合は、担持結晶としては四ホウ酸ナトリ
ウムおよびその水和物などが、塩水和物としてリン酸水
素二ナトリウム7水塩の場合は、担持結晶としてはリン
酸水素二ナトリウム2水塩などが例示される。
In the present invention, a crystal capable of supporting a salt hydrate is used as a supported crystal for a supercooling inhibitor. For example, when the salt hydrate is sodium acetate trihydrate, the supported crystals are disodium hydrogen phosphate, monosodium dihydrogen phosphate, trisodium phosphate, sodium tetraborate, sodium bromide, sodium sulfate, and salts thereof. Hydrates are exemplified. When strontium chloride hexahydrate is used as the salt hydrate, strontium hydroxide octahydrate is used as the supported crystal, and when the salt hydrate is disodium hydrogen phosphate dodecahydrate, the supported crystal is tetraborate. In the case where sodium acid and hydrates thereof are disodium hydrogen phosphate heptahydrate as a salt hydrate, examples of the supported crystals include disodium hydrogen phosphate dihydrate.

【0011】好ましくは、塩水和物として酢酸ナトリウ
ム3水塩、担持結晶としてリン酸水素二ナトリウム、リ
ン酸二水素一ナトリウム、リン酸三ナトリウム、四ホウ
酸ナトリウム、臭化ナトリウム、硫酸ナトリウムまたは
それらの水和物の組み合わせ、および塩水和物としてリ
ン酸水素二ナトリウム7水塩、担持結晶としてリン酸水
素二ナトリウム2水塩の組み合わせであり、さらに好ま
しくは、塩水和物として酢酸ナトリウム3水塩、担持結
晶としてリン酸水素二ナトリウムまたはリン酸三ナトリ
ウムが、特に好ましくは、塩水和物として酢酸ナトリウ
ム3水塩、担持結晶としてリン酸水素二ナトリウムが用
いられる。
Preferably, the salt hydrate is sodium acetate trihydrate, and the supported crystals are disodium hydrogen phosphate, monosodium dihydrogen phosphate, trisodium phosphate, sodium tetraborate, sodium bromide, sodium sulfate or a salt thereof. And a combination of disodium hydrogen phosphate heptahydrate as a salt hydrate and disodium hydrogen phosphate dihydrate as a supported crystal, more preferably sodium acetate trihydrate as a salt hydrate In particular, disodium hydrogen phosphate or trisodium phosphate is used as the supported crystal, particularly preferably sodium acetate trihydrate as the salt hydrate, and disodium hydrogen phosphate as the supported crystal.

【0012】本発明において、塩水和物の融液と過冷却
防止用担持結晶との混合物を製造するのに用いられる塩
水和物の融液は、塩水和物と必要に応じて加えられる水
との混合物を塩水和物の融点以上に加熱して製造され
る。必要に応じて加えられる水の量は水を加えたのちの
融液中の塩無水物換算濃度が室温(約25℃)における
飽和溶解度以上となるような範囲に限定される。室温に
おける飽和溶解度以下となるように多量の水を加えた場
合は、滴下液が全く固化しないか、固化しても強度が弱
いため好ましくない。塩水和物が酢酸ナトリウム3水塩
の場合は酢酸ナトリウム無水和物換算で20℃の飽和溶
液は31質量%であり、これより高濃度となるように水
が加えられる。水を全く添加しない場合は3水塩の無水
換算値60.0質量%となる。従って酢酸ナトリウムの
場合は32質量%〜60.0質量%、好ましくは40質
量%〜58質量%の範囲が融液濃度として好適である。
過冷却防止用担持結晶の混合物中における濃度は、混合
物中の溶解度を越える濃度以上で、90質量%以下であ
る。溶解度を下回ると溶解消失してしまうので担持結晶
としての役を果さない。90質量%を超えると、混合物
の流動性が乏しくなり、滴下に適さない。塩水和物が酢
酸ナトリウム3水塩の場合、過冷却防止用の担持結晶が
リン酸水素二ナトリウムの場合は、混合物に対して、3
〜90質量%,臭化ナトリウムの場合は20〜90質量
%,硫酸ナトリウムの場合は、10〜90質量%が例示
される。より好ましい範囲は、混合物の流動性の点か
ら、混合物に対して、担持結晶が20〜50質量%が好
適である。
In the present invention, the melt of the salt hydrate used for producing a mixture of the melt of the salt hydrate and the supporting crystals for preventing supercooling comprises a salt hydrate and water optionally added. Is heated above the melting point of the salt hydrate. The amount of water added as required is limited to a range such that the concentration in terms of salt anhydride in the melt after adding water is equal to or higher than the saturated solubility at room temperature (about 25 ° C.). If a large amount of water is added so as to have a saturation solubility at room temperature or less, it is not preferable because the dripping liquid does not solidify at all or the strength is low even after solidification. When the salt hydrate is sodium acetate trihydrate, the saturated solution at 20 ° C. in terms of sodium acetate anhydrate is 31% by mass, and water is added so as to have a higher concentration. When water is not added at all, the anhydrous equivalent of trihydrate is 60.0% by mass. Therefore, in the case of sodium acetate, a range of 32% by mass to 60.0% by mass, preferably 40% by mass to 58% by mass is suitable as a melt concentration.
The concentration of the supporting crystals for preventing supercooling in the mixture is not less than the concentration exceeding the solubility in the mixture and not more than 90% by mass. When the solubility is lower than the solubility, the compound is dissolved and disappears, and thus does not serve as a supported crystal. If it exceeds 90% by mass, the fluidity of the mixture becomes poor, making it unsuitable for dropping. When the salt hydrate is sodium acetate trihydrate, and when the supported crystal for preventing supercooling is disodium hydrogen phosphate, 3
To 90% by mass, 20 to 90% by mass for sodium bromide, and 10 to 90% by mass for sodium sulfate. A more preferable range is that, from the viewpoint of the fluidity of the mixture, the amount of the supported crystals is 20 to 50% by mass based on the mixture.

【0013】塩水和物の融液と過冷却防止用担持結晶と
の混合物中における担持結晶の沈降を防止するために増
粘剤を加えることができる。これによって滴下液の均質
性を向上させることができる。用いられる増粘剤として
はカルボキシメチルセルロース,ポリアクリル酸ナトリ
ウムなどの高分子系増粘剤,高吸水性樹脂,微粉末シリ
カなどから、塩水和物に対して増粘作用のあるものを選
択すればよい。塩水和物が酢酸ナトリウム3水塩の場合
は、カルボキシメチルセルロース,部分加水分解ポリア
クリルアミドなどが好適に用いられる。
[0013] A thickener may be added in order to prevent sedimentation of the supported crystals in the mixture of the melt of the salt hydrate and the supported crystals for preventing supercooling. Thereby, the homogeneity of the dripping liquid can be improved. As a thickener to be used, a polymer thickener such as carboxymethylcellulose, sodium polyacrylate, etc., a superabsorbent resin, finely divided silica, etc., which has a thickening effect on salt hydrate can be selected. Good. When the salt hydrate is sodium acetate trihydrate, carboxymethylcellulose, partially hydrolyzed polyacrylamide and the like are preferably used.

【0014】塩水和物の融液と過冷却防止用担持結晶と
の混合物を保持する温度範囲は、塩水和物と必要に応じ
て加えられた水との混合物中の塩水和物の融点以上であ
る。酢酸ナトリウム3水塩の水溶液の場合は、水の量に
も依存するが、50〜70℃、より好ましくは55〜6
5℃が例示される。70℃を超えても不都合はないが、
余り高温の場合に水分の蒸散があるので必要以上に加熱
するのは好ましくない。
The temperature range in which the mixture of the melt of the salt hydrate and the supporting crystals for preventing supercooling is maintained is not lower than the melting point of the salt hydrate in the mixture of the salt hydrate and water added as required. is there. In the case of an aqueous solution of sodium acetate trihydrate, it depends on the amount of water, but is preferably from 50 to 70C, more preferably from 55 to 6O <0> C.
5 ° C. is exemplified. Although there is no inconvenience even if it exceeds 70 ° C,
If the temperature is too high, there is evaporation of water, so it is not preferable to heat more than necessary.

【0015】本発明において揆水性材料としては、樹
脂、金属、陶器など通常用いられる多くの材料が支障な
く用いられる。形状はフィルム、シート,板,トレーな
ど必要に応じて選択できる。
In the present invention, as the water-repellent material, many commonly used materials such as resin, metal and ceramics can be used without any trouble. The shape can be selected as needed, such as a film, a sheet, a plate, and a tray.

【0016】塩水和物の融液と過冷却防止用担持結晶と
の混合物の液滴を形成する方法としては、混合物の液流
を断続的に流下させる方法、多孔板や網などを通過させ
る方法などがある。また液流を生成させるには自然流下
式、ポンプ圧送式などの方法がある。揆水性材料の上に
液滴を形成するには液の供給側か揆水性材料いずれかが
移動する必要があるが、通常の工学的判断で選択すれば
よい。
As a method for forming droplets of a mixture of a melt of a salt hydrate and a supporting crystal for preventing supercooling, a method of intermittently flowing a liquid flow of the mixture, a method of passing through a perforated plate or a net, etc. and so on. In addition, there are methods of generating a liquid flow such as a natural flow type and a pump pressure type. In order to form droplets on the repellent material, either the liquid supply side or the repellent material needs to move, which may be selected by ordinary engineering judgment.

【0017】該液滴を形成して後に固化させるには、放
冷または強制冷却する。冷却しても固化しない液滴があ
る場合は、塩水和物の微細結晶を微量添加すると直ちに
固化する。この微細結晶を予め揆水性材料に散布してお
くと、未硬化率は著しく低減できる。
In order to form the droplets and solidify them later, the droplets are cooled or forcedly cooled. If there are droplets that do not solidify even after cooling, they solidify immediately upon addition of a minute amount of fine crystals of the salt hydrate. If these fine crystals are sprayed on a water-based material in advance, the uncured rate can be significantly reduced.

【0018】液滴を固化させると顆粒が得られる。顆粒
の大きさは液滴の大きさで決定され、所望の大きさを選
択すればよい。通常は充填容器の注入孔の大きさよりも
小さいことが要求される。顆粒の大きさは直径3〜15
mmの範囲が好ましい。顆粒の形状は、液滴の形状で決
定されるが、粘度の高い液滴の場合は球形に近くなり、
粘度の低い液滴の場合は平板状に近くなる。いずれの形
状でも過冷却防止効果には差違はない。
When the droplets are solidified, granules are obtained. The size of the granule is determined by the size of the droplet, and a desired size may be selected. Usually, it is required to be smaller than the size of the injection hole of the filling container. The size of the granules is 3 to 15 in diameter
The range of mm is preferred. The shape of the granules is determined by the shape of the droplets, but in the case of highly viscous droplets, they are close to spherical,
In the case of a liquid droplet having a low viscosity, the liquid droplet becomes almost flat. In any case, there is no difference in the effect of preventing supercooling.

【0019】本発明の過冷却防止剤顆粒は、蓄熱材融液
が充填されたあと、容器内で確実に固化させるために用
いられる。蓄熱材融液が充填される前に容器に予め顆粒
を添加しておくことができる。また蓄熱材融液が容器に
充填されたあとに顆粒を添加することもできる。添加さ
れる顆粒は1個で十分であるが、容器の大きさによって
複数個でも支障はない。
The supercooling inhibitor granules of the present invention are used to reliably solidify in the container after the heat storage material melt is filled. The granules can be added to the container before the heat storage material melt is filled. Granules can also be added after the heat storage material melt is filled in a container. One granule to be added is sufficient, but a plurality of granules does not matter depending on the size of the container.

【0020】本発明の過冷却防止剤顆粒を用いる蓄熱材
は、蓄熱材主材である塩水和物、必要に応じて添加され
る融点調整剤、過冷却防止剤、および固液分離防止剤な
どからなる組成物の融液に該顆粒を添加して調製され
る。この際に蓄熱材主材である塩水和物と、該顆粒の塩
水和物とは同一物である必要がある。蓄熱材はパネル状
あるいは管状などの容器に充填・シールされて用いられ
る。本発明の過冷却防止剤顆粒を用いる蓄熱装置は、上
記のようにして調製され、容器に充填された蓄熱材と電
熱ヒーターなどの発熱体および断熱材などから構成され
る。これらの全部または一部が一体化したもの、あるい
は個別のものを施工現場で順次設置して用いられる。床
暖房の場合を例示すると、下から順に、床構造材/断熱
材/発熱体/蓄熱材/床材/床仕上材の構成とするのが
一般的である。
The heat storage material using the supercooling inhibitor granules of the present invention includes salt hydrate, which is a main material of the heat storage material, a melting point regulator, a supercooling inhibitor, and a solid-liquid separation inhibitor added as needed. By adding the granules to a melt of a composition comprising At this time, the salt hydrate, which is the main material of the heat storage material, and the salt hydrate of the granules need to be the same. The heat storage material is used after being filled and sealed in a panel-like or tubular container. The heat storage device using the supercooling inhibitor granules of the present invention is composed of a heat storage material prepared as described above and filled in a container, a heating element such as an electric heater, a heat insulating material, and the like. All or some of them are integrated or individual ones are sequentially installed and used at the construction site. Taking the case of floor heating as an example, it is common to have a structure of floor structural material / heat insulating material / heating element / heat storage material / floor material / floor finishing material in order from the bottom.

【0021】[0021]

【実施例】以下実施例により本発明を具体的に説明する
が、本発明はこれらに限定されるものではない。
EXAMPLES The present invention will be described in more detail with reference to the following Examples, but it should not be construed that the invention is limited thereto.

【0022】実施例1 50mlビーカーに酢酸ナトリウム(無水)9.72
g,水8.28gをとり、60℃水浴中で加熱して酢酸
ナトリウム54質量%融液を調製した。これにリン酸水
素二ナトリウム(無水)12.00gを添加して30分
攪拌した。攪拌を継続しながらスポイトでスラリーを吸
い上げ、予めトレイの中に敷いたポリエチレンフィルム
上に滴下する操作を数回繰り返した結果、122個の液
滴が形成された。滴下30分後に液滴のうち硬化したも
のは98%(硬化率)であった。これをトレイのまま7
℃恒温器に入れ、2時間後に取り出すと、硬化率は10
0%であった。このようにして得られた顆粒を以下の融
液中安定性テストに供した。酢酸ナトリウム56質量
%,リン酸水素二ナトリウム2質量%、残部水からなる
融液(62℃)30gをガラススクリュー管に入れ、6
2℃水浴に浸漬した。これに顆粒1個を入れ、62℃で
6時間保持した。顆粒の外形の変化はなかった。その
後、水浴に入れたままで水浴の加熱を停止し、放冷し
た。30分後に水温は37℃となり、ガラススクリュー
管中の融液は固化していた。顆粒の過冷却防止剤として
の効果が確認された。
Example 1 9.72 sodium acetate (anhydrous) in a 50 ml beaker
g and 8.28 g of water, and heated in a 60 ° C. water bath to prepare a 54% by mass sodium acetate melt. To this, 12.00 g of disodium hydrogen phosphate (anhydrous) was added and stirred for 30 minutes. The operation of sucking up the slurry with a dropper while continuing stirring and dropping the slurry on a polyethylene film previously laid in a tray was repeated several times, and as a result, 122 droplets were formed. After 30 minutes from the dropping, 98% of the droplets were cured (curing rate). Leave this in the tray 7
When placed in a constant temperature oven and taken out after 2 hours, the curing rate is 10
It was 0%. The granules thus obtained were subjected to the following melt stability test. 30 g of a melt (62 ° C.) composed of 56% by mass of sodium acetate, 2% by mass of disodium hydrogen phosphate and the balance of water was placed in a glass screw tube,
It was immersed in a 2 ° C. water bath. One granule was added thereto and kept at 62 ° C. for 6 hours. There was no change in the shape of the granules. Thereafter, the heating of the water bath was stopped while being kept in the water bath, and the solution was allowed to cool. After 30 minutes, the water temperature reached 37 ° C., and the melt in the glass screw tube had solidified. The effect of the granules as a supercooling inhibitor was confirmed.

【0023】実施例2〜11,比較例1〜3 実施例1と同様にして酢酸ナトリウム融液の濃度とリン
酸水素二ナトリウム濃度の異なる混合物を調製し、ポリ
エチレンフィルム上に滴下して、液滴の硬化率と得られ
た顆粒の融液中安定性テストを実施した。以上の結果を
表1に示す。
Examples 2 to 11 and Comparative Examples 1 to 3 In the same manner as in Example 1, a mixture having a different concentration of sodium acetate melt and a different concentration of disodium hydrogen phosphate was prepared, and the mixture was dropped on a polyethylene film. The drop cure rate and the stability of the resulting granules in the melt were tested. Table 1 shows the above results.

【0024】[0024]

【表1】 [Table 1]

【0025】[0025]

【発明の効果】本発明によれば、塩水和物の過冷却防止
剤の製造方法において、経済性、安全性、簡便性におい
て優れた製造方法が開示され、例えば、塩水和物を主材
とする蓄熱材の製造に寄与するところ大である。
According to the present invention, there is disclosed a method for producing a supercooling inhibitor for salt hydrate which is excellent in economy, safety and simplicity. It greatly contributes to the production of heat storage materials.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】塩水和物の融液と過冷却防止用担持結晶と
の混合物を融点以上に保持して揆水性材料の上に液滴を
形成後、該混合物を冷却固化させることを特徴とする塩
水和物の過冷却防止剤顆粒の製造方法。
The present invention is characterized in that a mixture of a melt of a salt hydrate and a supporting crystal for preventing supercooling is maintained at a melting point or higher to form droplets on an aqueous material, and the mixture is cooled and solidified. For producing supercooling inhibitor granules of salt hydrate.
【請求項2】増粘剤が更に添加された混合物を用いるこ
とからなる請求項1記載の塩水和物の過冷却防止剤顆粒
の製造方法。
2. The method for producing a superhydrate inhibitor granule of a salt hydrate according to claim 1, wherein the mixture further comprises a thickener.
【請求項3】揆水性材料の上に予め塩水和物結晶を存在
させておき、その上に混合物を滴下して液滴を形成する
請求項1記載の塩水和物の過冷却防止剤顆粒の製造方
法。
3. The method of claim 1, wherein the salt hydrate crystals are pre-existing on the water-repellent material, and the mixture is dropped thereon to form droplets. Production method.
【請求項4】揆水性材料の上に滴下して液滴を形成させ
た後、液滴に塩水和物結晶を添加して冷却固化させる請
求項1記載の塩水和物の過冷却防止剤顆粒の製造方法。
4. The supercooling inhibitor granules for salt hydrate according to claim 1, wherein the droplets are dropped on the repellent material to form droplets, and then the salt hydrate crystals are added to the droplets to solidify by cooling. Manufacturing method.
【請求項5】請求項1〜4のいずれかに記載の製造方法
にて製造される塩水和物の過冷却防止剤顆粒を用いる蓄
熱材又は蓄熱装置。
5. A heat storage material or a heat storage device using supercooling inhibitor granules of a salt hydrate produced by the production method according to any one of claims 1 to 4.
JP2000213916A 2000-07-14 2000-07-14 Method for producing granule of agent for preventing supercooling of salt hydrate Pending JP2002030280A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publication Number Publication Date
JP2002030280A true JP2002030280A (en) 2002-01-31

Family

ID=18709590

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Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015163200A1 (en) * 2014-04-24 2015-10-29 シャープ株式会社 Method for producing heat storage member
US20210130748A1 (en) * 2018-07-17 2021-05-06 Henkel Ag & Co. Kgaa Solid Fragrance-Containing Composition

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JPS5774380A (en) * 1980-10-27 1982-05-10 Matsushita Electric Ind Co Ltd Production of supercooling inhibitor
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JPS57177086A (en) * 1981-04-24 1982-10-30 Matsushita Electric Works Ltd Heat storing material
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JPS6044033A (en) * 1983-07-29 1985-03-08 サントレ−ド・リミテツド Granule producing apparatus
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JPH10237434A (en) * 1997-02-28 1998-09-08 Sumika Plast Kk Production of heat storage material
JPH10298543A (en) * 1997-02-28 1998-11-10 Sumika Plus Tec Kk Production of supercooling inhibitor for salt hydrate
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JPS5719596A (en) * 1980-07-09 1982-02-01 Mitsubishi Electric Corp Regenerator
JPS5731982A (en) * 1980-08-05 1982-02-20 Sekisui Chem Co Ltd Heat-accumulating agent composition
JPS5774380A (en) * 1980-10-27 1982-05-10 Matsushita Electric Ind Co Ltd Production of supercooling inhibitor
JPS5790589A (en) * 1980-11-22 1982-06-05 Matsushita Electric Works Ltd Heat accumulating device
JPS57177086A (en) * 1981-04-24 1982-10-30 Matsushita Electric Works Ltd Heat storing material
JPS57180685A (en) * 1981-04-30 1982-11-06 Matsushita Electric Works Ltd Heat accumulating material
JPS57180684A (en) * 1981-04-30 1982-11-06 Matsushita Electric Works Ltd Heat accumulating material
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JPS6475583A (en) * 1987-09-18 1989-03-22 Nok Corp Preparation of nucleating agent
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JPH0680956A (en) * 1992-09-04 1994-03-22 Mitsubishi Petrochem Co Ltd Heat storage composition and its production
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JPH10298543A (en) * 1997-02-28 1998-11-10 Sumika Plus Tec Kk Production of supercooling inhibitor for salt hydrate
JPH11276877A (en) * 1998-02-27 1999-10-12 Sandvik Ab Dropping molding and apparatus therefor

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015163200A1 (en) * 2014-04-24 2015-10-29 シャープ株式会社 Method for producing heat storage member
US20210130748A1 (en) * 2018-07-17 2021-05-06 Henkel Ag & Co. Kgaa Solid Fragrance-Containing Composition

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