JPH0470927B2 - - Google Patents
Info
- Publication number
- JPH0470927B2 JPH0470927B2 JP60255856A JP25585685A JPH0470927B2 JP H0470927 B2 JPH0470927 B2 JP H0470927B2 JP 60255856 A JP60255856 A JP 60255856A JP 25585685 A JP25585685 A JP 25585685A JP H0470927 B2 JPH0470927 B2 JP H0470927B2
- Authority
- JP
- Japan
- Prior art keywords
- calcium chloride
- weight
- desiccant
- moisture absorption
- powder
- 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
Links
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims description 34
- 239000001110 calcium chloride Substances 0.000 claims description 31
- 229910001628 calcium chloride Inorganic materials 0.000 claims description 31
- 239000000843 powder Substances 0.000 claims description 26
- 239000002274 desiccant Substances 0.000 claims description 20
- 239000002245 particle Substances 0.000 claims description 15
- 238000002156 mixing Methods 0.000 claims description 9
- 239000006260 foam Substances 0.000 claims description 7
- 238000010521 absorption reaction Methods 0.000 description 17
- 239000007788 liquid Substances 0.000 description 12
- 230000007423 decrease Effects 0.000 description 10
- 230000000694 effects Effects 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 238000001035 drying Methods 0.000 description 4
- 239000006185 dispersion Substances 0.000 description 3
- 229910001562 pearlite Inorganic materials 0.000 description 3
- 229920006395 saturated elastomer Polymers 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 239000010455 vermiculite Substances 0.000 description 2
- 229910052902 vermiculite Inorganic materials 0.000 description 2
- 235000019354 vermiculite Nutrition 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000006261 foam material Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000010451 perlite Substances 0.000 description 1
- 235000019362 perlite Nutrition 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Landscapes
- Drying Of Gases (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Description
[産業上の利用分野]
本発明は、塩化カルシウムを用いた新規な乾燥
剤に関する。詳しくは、優れた吸湿性を有し、且
つ塩化カルシウムの潮解液の流出を防止した乾燥
剤である。
[従来の技術および問題点]
塩化カルシウムは、高い吸湿性を有するため、
乾燥剤として広く使用されている。例えば、上記
塩化カルシウムを、通気性シートよりなる蓋を有
する容器に充填して使用する態様が最も一般に行
われている。
しかしながら、上記塩化カルシウムを用いた乾
燥剤は、ある程度吸湿が進むと、吸湿速度が大き
く低下し、これから飽和吸湿量に達するまでの間
の乾燥効果が充分得られないという問題を有す
る。また、塩化カルシウムの潮解液が生成し、該
液の流出に対し、取扱上の制約があつた。
[発明が解決しようとする問題点]
本発明者等は、かかる問題を解決すべく鋭意研
究を重ねた。その結果、乾燥状態の塩化カルシウ
ムに特定の粉体を混合したものを乾燥剤として用
いることにより、塩化カルシウムにおける吸湿速
度の低下が少なく、安定した吸湿性を示し、しか
も塩化カルシウムの単位重量あたりの吸湿量が飛
躍的に向上すること、および前記潮解液の流出を
効果的に防止し得ることを見い出し、本発明を完
成するに至つた。
本発明は、4メツシユふるい通過粒子80重量%
以上で、且つ100メツシユふるい通過粒子50重量
%以下の粒度を有する『無機質発泡体の粉砕物
(以下、発泡粉体ともいう)』100重量部に対して、
20〜300重量部の塩化カルシウム粉末を分散混合
してなる乾燥剤である。
本発明において、発泡粉体としてはパーライ
ト、バーミキユライト等の鉱物を焼成して得られ
る発泡体、シラスバルーン等の天然発泡体等の発
泡倍率が一般に10〜40である無機質発泡体を粉砕
したものが好適に用いられる。これらの発泡粉体
のうち、特にパーライト(真珠岩系)および/ま
たバーミキユライトの発泡体を粉砕したものが、
本発明の効果に顕著であり好ましい。また、発泡
粉体の粒度は、4メツシユふるい通過粒子が80重
量%、さらに好ましくは90重量%以上で、且つ
100メツシユふるい通過粒子が50重量%以下、好
ましくは40重量%以下であることが望ましい。即
ち、4メツシユふるい通過粒子の割合が前記範囲
より少ない場合には、粒子間の液の拡散性が低下
するため、得られる乾燥剤の吸湿速度および吸湿
量が低下する傾向を示す。また、100メツシユふ
るい通過粒子の割合が前記範囲より多い場合に
は、粒子間の液の拡散が低下するため、同様に吸
湿速度が低下すると共に、保水性の低下に伴い、
得られる乾燥剤の吸湿量も低下する傾向がある。
また、塩化カルシウムとしては粉状、粒状、フ
レーク状等の形状のものがあるが、本発明におい
ては、そのうち、粉状の塩化カルシウムを使用す
ることが、塩化カルシウムの表面積を増大させ
て、吸湿速度を向上できると共に、後記する発泡
粉体中に分散混合後の層分離も少なく好適であ
る。
本発明において、発泡粉体に対する塩化カルシ
ウムの混合割合は、発泡粉体100重量部に対して
塩化カルシウム20〜300重量部、好ましくは50〜
250重量部の割合が適当である。塩化カルシウム
の割合が上記範囲より多い場合には、塩化カルシ
ウムの潮解液の全量を発泡粉体中に拡散及び保持
することが困難となるため、吸湿速度の低下ある
いは潮解液の浸出が生じる傾向がある。また、塩
化カルシウムの割合が上記範囲より少ない場合に
は、特に吸湿性に影響はないが、乾燥剤の体積が
必要以上に大きくなり、また経済的でない。
本発明において、発泡粉体と塩化カルシウムと
の混合は、乾燥状態で行うことが優れた乾燥剤を
得るために重要であり、このような混合を分散混
合という。これに対して、塩化カルシウムを一担
水溶液とし、これを発泡粉体に吸収させた後、乾
燥して得られた乾燥剤では、本発明のような優れ
た吸湿性が発揮されない。即ち、このような乾燥
剤では塩化カルシウムの潮解液の拡散に有効な発
泡粉体の細孔あるいは形状が、乾燥後の塩化カル
シウムによつて変化するためと思われる。また、
本発明において、分散混合は塩化カルシウムが発
泡粉体中に均一に分散している態様が最も好まし
いが、該塩化カルシウムの一部が発泡粉体中に偏
在している態様であつてもよく、この場合でも充
分効果を発揮し得る。
本発明の乾燥剤の使用態様は、特に制限されな
い。代表的な使用態様を例示すれば、少なくとも
一部に吸湿性を有する容器(シートによつて形成
される袋を含む)に充填する態様、デシケータ等
の密閉容器内に充填する態様等が挙げられる。ま
た、成型助剤、例えばケイ散カルシウム等を加え
て圧縮成型等の成型方法により、任意の形状に成
形してもよい。
[効果および作用]
以上の説明より理解されるように、本発明の乾
燥剤は、飽和吸湿量に達するまでに吸湿速度の低
下が極めて少なく、しかも飽和吸湿量が従来の塩
化カルシウムを用いた乾燥剤では予想されない程
に高い値を示すものである。因に、吸湿量は塩化
カルシウム単独の場合に比べて2倍以上である。
また、潮解液は発泡粉体中に保持されるため、潮
解液の流出もほとんどないという特徴をも有す
る。
本発明の乾燥剤が上記した優れた吸湿性を発揮
する作用機構は明らかではないが、本発明者等
は、発泡粉体の特異な凹凸および細孔の構造によ
り、該粉体が単に保水性を有するのみでなく、水
を拡散する機能を有しており、これにより吸湿の
過程で塩化カルシウム表面で生成する潮解液が速
やかに拡散され保持されるため、塩化カルシウム
表面が潮解液層で覆われることなく、該表面を常
に高い塩化カルシウム濃度に維持し得ることによ
るものと推定している。
[実施例]
以下、本発明を具体的に説明するため実施例を
示すが、本発明はこれらの実施例に限定されるも
のではない。
尚、実施例および比較例において、吸湿性試験
は、試料100gを温度20℃、湿度80%の室内に置
き、7日後、14日後、21日後、28日後における重
量の増加量を測定したものを吸湿量として示し
た。また、上記増加量を塩化カルシウム100g当
りの量に換算したものを単位吸湿量として示し
た。
実施例 1
第1表に示す発泡粉体を使用し、この発泡粉体
100重量部に対して、第2表に示す割合で無水塩
化カルシウム粉末ブレンダーで混合して乾燥剤を
得た。これらの乾燥剤の吸湿試験の結果を第2表
に併せて示す。尚、第2表のNo.6は潮解液の浸出
が生じた。
[Industrial Application Field] The present invention relates to a novel desiccant using calcium chloride. Specifically, it is a desiccant that has excellent hygroscopicity and prevents the deliquescent solution of calcium chloride from flowing out. [Prior art and problems] Calcium chloride has high hygroscopicity, so
Widely used as a desiccant. For example, the most common method is to fill a container with a lid made of a breathable sheet with the calcium chloride. However, the desiccant using calcium chloride has the problem that once moisture absorption progresses to a certain extent, the moisture absorption rate decreases significantly, and a sufficient drying effect cannot be obtained until the saturated moisture absorption amount is reached. In addition, a deliquescent liquid of calcium chloride was generated, and there were restrictions on handling the outflow of the liquid. [Problems to be Solved by the Invention] The present inventors have conducted extensive research in order to solve these problems. As a result, by using a mixture of dry calcium chloride and a specific powder as a desiccant agent, calcium chloride showed stable hygroscopicity with little decrease in moisture absorption rate, and moreover, The present inventors have discovered that the amount of moisture absorption can be dramatically improved and that the outflow of the deliquescent liquid can be effectively prevented, leading to the completion of the present invention. In the present invention, 80% by weight of particles passing through a 4-mesh sieve
With respect to 100 parts by weight of "pulverized inorganic foam material (hereinafter also referred to as foamed powder)" having a particle size of 50% by weight or less of particles passing through a 100-mesh sieve,
This desiccant is made by dispersing and mixing 20 to 300 parts by weight of calcium chloride powder. In the present invention, the foamed powder is a pulverized inorganic foam whose expansion ratio is generally 10 to 40, such as a foam obtained by firing minerals such as perlite and vermiculite, and a natural foam such as Shirasu balloon. are preferably used. Among these foamed powders, especially crushed pearlite and/or vermiculite foams,
The effect of the present invention is remarkable and preferable. Further, the particle size of the foamed powder is such that the particles passing through a 4-mesh sieve account for 80% by weight, more preferably 90% by weight or more, and
It is desirable that the amount of particles passing through a 100 mesh sieve is not more than 50% by weight, preferably not more than 40% by weight. That is, when the proportion of particles passing through the four-mesh sieve is less than the above range, the diffusivity of liquid between particles decreases, so that the moisture absorption rate and amount of moisture absorption of the resulting desiccant tends to decrease. In addition, if the proportion of particles passing through a 100-mesh sieve is greater than the above range, the diffusion of liquid between particles will decrease, and the moisture absorption rate will similarly decrease, as well as the water retention capacity will decrease.
The amount of moisture absorption of the resulting desiccant also tends to decrease. In addition, calcium chloride can be in the form of powder, granules, flakes, etc., but in the present invention, using powdered calcium chloride increases the surface area of calcium chloride and absorbs moisture. It is preferable that the speed can be improved and that layer separation after dispersion and mixing in the foamed powder described later is small. In the present invention, the mixing ratio of calcium chloride to the foamed powder is 20 to 300 parts by weight, preferably 50 to 300 parts by weight, per 100 parts by weight of the foamed powder.
A proportion of 250 parts by weight is suitable. If the proportion of calcium chloride is higher than the above range, it will be difficult to diffuse and retain the entire amount of calcium chloride deliquescent liquid in the foamed powder, so there will be a tendency for the moisture absorption rate to decrease or for the deliquescent liquid to seep out. be. Further, if the proportion of calcium chloride is less than the above range, there is no particular effect on hygroscopicity, but the volume of the desiccant becomes larger than necessary, and it is not economical. In the present invention, it is important to mix the foamed powder and calcium chloride in a dry state in order to obtain an excellent desiccant, and such mixing is called dispersion mixing. On the other hand, a desiccant obtained by making a monocarboxylic aqueous solution of calcium chloride, absorbing it into a foamed powder, and then drying it does not exhibit the excellent hygroscopicity as in the present invention. That is, in such a desiccant, it is thought that the pores or shape of the foamed powder, which are effective for diffusing the deliquescent liquid of calcium chloride, change depending on the calcium chloride after drying. Also,
In the present invention, the dispersion mixing is most preferably carried out in such a manner that calcium chloride is uniformly dispersed in the foamed powder, but it may also be carried out in such a manner that a portion of the calcium chloride is unevenly distributed in the foamed powder. Even in this case, sufficient effects can be achieved. The manner in which the desiccant of the present invention is used is not particularly limited. Typical usage patterns include filling a container at least partially hygroscopic (including a bag formed of a sheet), filling a closed container such as a desiccator, etc. . Further, it may be molded into an arbitrary shape by adding a molding aid such as calcium silica and the like by a molding method such as compression molding. [Effects and Actions] As can be understood from the above explanation, the desiccant of the present invention has an extremely small decrease in the moisture absorption rate until reaching the saturated moisture absorption amount, and the saturated moisture absorption amount is lower than that of conventional drying using calcium chloride. This value is unexpectedly high for agents. Incidentally, the amount of moisture absorbed is more than twice that of calcium chloride alone.
Furthermore, since the deliquescent liquid is retained in the foamed powder, it also has the characteristic that there is almost no outflow of the deliquescent liquid. Although the mechanism by which the desiccant of the present invention exhibits the above-mentioned excellent hygroscopicity is not clear, the present inventors believe that the unique unevenness and pore structure of the foamed powder makes it possible for the powder to simply retain water. In addition to having a water-diffusing function, the deliquescent liquid that forms on the surface of calcium chloride during moisture absorption is quickly diffused and retained, so that the calcium chloride surface is covered with a layer of deliquescent liquid. It is presumed that this is due to the fact that the surface can always maintain a high calcium chloride concentration without being affected. [Examples] Examples are shown below to specifically explain the present invention, but the present invention is not limited to these Examples. In addition, in the Examples and Comparative Examples, the hygroscopic test was performed by placing 100g of the sample in a room with a temperature of 20°C and a humidity of 80%, and measuring the increase in weight after 7 days, 14 days, 21 days, and 28 days. It is shown as the amount of moisture absorbed. In addition, the above-mentioned increased amount was converted into the amount per 100 g of calcium chloride and was shown as the unit moisture absorption amount. Example 1 Using the foamed powder shown in Table 1, this foamed powder
A desiccant was obtained by mixing 100 parts by weight with an anhydrous calcium chloride powder blender in the proportions shown in Table 2. The results of the moisture absorption test for these desiccants are also shown in Table 2. Incidentally, in No. 6 in Table 2, leaching of deliquescent fluid occurred.
【表】【table】
【表】
比較例 1
塩化カルシウム100gについて、吸湿性試験を
行つた結果、吸水量は、7日で180g、14日で224
g、21日で240g、28日で270gであつた。
比較例 2
実施例1で使用した発泡粉体A100重量部に対
して塩化カルシウム100重量部の割合となるよう
に、該発泡粉体に塩化カルシウム水溶液を含浸さ
せた後、乾燥して乾燥後を得た。得られた乾燥剤
について吸湿性試験を行つた。その結果を第3表
に示す。[Table] Comparative Example 1 As a result of conducting a hygroscopic test on 100g of calcium chloride, the amount of water absorbed was 180g in 7 days and 224g in 14 days.
g, 240 g on the 21st, and 270 g on the 28th. Comparative Example 2 The foamed powder was impregnated with an aqueous calcium chloride solution at a ratio of 100 parts by weight of calcium chloride to 100 parts by weight of the foamed powder A used in Example 1, and then dried. Obtained. A hygroscopicity test was conducted on the obtained desiccant. The results are shown in Table 3.
【表】
比較例 3
実施例1で使用したパーライト発泡体を粉砕せ
ずに用いて、実施例1のBと同じように4メツシ
ユ通過粒子100重量%、100メツシユ通過粒子30重
量%となるようなパーライト発泡体を選び、該非
粉砕パーライト発泡体100重量部に対して、無水
塩化カルシウム粉末100重量部(実施例1のNo.7
と同条件)をブレンダーで混合して得た乾燥剤の
吸湿試験の結果を第4表に示す。[Table] Comparative Example 3 The pearlite foam used in Example 1 was used without being crushed, and as in B of Example 1, the particles passing through 4 meshes were 100% by weight and the particles passing through 100 meshes were 30% by weight. 100 parts by weight of anhydrous calcium chloride powder (No. 7 of Example 1) was added to 100 parts by weight of the non-pulverized pearlite foam.
Table 4 shows the results of the moisture absorption test of the desiccant obtained by mixing (same conditions as above) in a blender.
Claims (1)
つ100メツシユふるい通過粒子50重量%以下の粒
度を有する『無機質発泡体の粉砕物』100重量部
に対して、20〜300重量部の塩化カルシウム粉末
を分散混合してなる乾燥剤。1 20 to 300 parts by weight of calcium chloride powder is added to 100 parts by weight of "pulverized inorganic foam" having a particle size of 80% by weight or more of particles passing through a 4-mesh sieve and 50% by weight or less of particles passing through a 100-mesh sieve. A desiccant made by dispersing and mixing.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25585685A JPS62117614A (en) | 1985-11-16 | 1985-11-16 | Drying agent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25585685A JPS62117614A (en) | 1985-11-16 | 1985-11-16 | Drying agent |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62117614A JPS62117614A (en) | 1987-05-29 |
JPH0470927B2 true JPH0470927B2 (en) | 1992-11-12 |
Family
ID=17284536
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP25585685A Granted JPS62117614A (en) | 1985-11-16 | 1985-11-16 | Drying agent |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62117614A (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0659383B2 (en) * | 1987-12-11 | 1994-08-10 | 小野田セメント株式会社 | Complex desiccant |
KR100406748B1 (en) * | 2001-07-18 | 2003-11-21 | 주식회사 새남소재 | Desiccant by using the natural mineral and the calcium chloride (or magnesium chloride) and its manufacturing process |
KR100418100B1 (en) * | 2001-09-15 | 2004-02-11 | 강용성 | The absorber manufacturing method |
US6652775B2 (en) | 2001-11-29 | 2003-11-25 | Multisorb Technologies, Inc. | Adsorbent compositions |
US6540937B1 (en) | 2001-11-29 | 2003-04-01 | Multisorb Technologies, Inc. | Adsorbent compositions |
Citations (7)
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---|---|---|---|---|
JPS52107042A (en) * | 1976-03-05 | 1977-09-08 | Japan Synthetic Rubber Co Ltd | Hygroscopic composition |
JPS57105237A (en) * | 1980-12-24 | 1982-06-30 | Tokuyama Soda Co Ltd | Drying agent |
JPS57136934A (en) * | 1981-02-19 | 1982-08-24 | Yoshihiko Yamagami | Deoxidizing desiccating agent |
JPS57144021A (en) * | 1981-03-04 | 1982-09-06 | Shin Nisso Kako Co Ltd | Desiccating agent for high humidity |
JPS58219919A (en) * | 1982-06-15 | 1983-12-21 | Shin Nisso Kako Co Ltd | Drying composition and package |
JPS59193133A (en) * | 1983-04-18 | 1984-11-01 | Kaken Pharmaceut Co Ltd | Drying agent |
JPS61216715A (en) * | 1985-03-19 | 1986-09-26 | Shin Nisso Kako Co Ltd | Drying composition and package |
-
1985
- 1985-11-16 JP JP25585685A patent/JPS62117614A/en active Granted
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52107042A (en) * | 1976-03-05 | 1977-09-08 | Japan Synthetic Rubber Co Ltd | Hygroscopic composition |
JPS57105237A (en) * | 1980-12-24 | 1982-06-30 | Tokuyama Soda Co Ltd | Drying agent |
JPS57136934A (en) * | 1981-02-19 | 1982-08-24 | Yoshihiko Yamagami | Deoxidizing desiccating agent |
JPS57144021A (en) * | 1981-03-04 | 1982-09-06 | Shin Nisso Kako Co Ltd | Desiccating agent for high humidity |
JPS58219919A (en) * | 1982-06-15 | 1983-12-21 | Shin Nisso Kako Co Ltd | Drying composition and package |
JPS59193133A (en) * | 1983-04-18 | 1984-11-01 | Kaken Pharmaceut Co Ltd | Drying agent |
JPS61216715A (en) * | 1985-03-19 | 1986-09-26 | Shin Nisso Kako Co Ltd | Drying composition and package |
Also Published As
Publication number | Publication date |
---|---|
JPS62117614A (en) | 1987-05-29 |
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