JP2008289955A - Humidity-conditioning gas-absorbing agent and humidity-conditioning gas-absorbing implement - Google Patents
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この発明は、調湿機能と酸性ガスの捕捉吸着機能を備えた調湿吸ガス剤、および、調湿対象となる空間内に静置されて、この空間内の調湿をなすと同時にこの空間内にある酸性ガスを捕捉吸着して、この空間内にある物品の劣化を防止する調湿吸ガス具に関する。 The present invention relates to a humidity-controlling agent having a humidity-control function and an acid-gas capturing / adsorption function, and being placed in a space to be humidity-controlled to simultaneously control the humidity in this space. The present invention relates to a humidity-controlled gas-absorbing device that captures and adsorbs acidic gas in the interior and prevents deterioration of articles in the space.
ある空間において、調湿と酸性ガスの除去とが同時に必要とされるような場合には、一般に、この空間内にシリカゲルなどの調湿剤を静置させると共に、酸性ガスの化学吸着剤を静置させる手法が採られる。 When humidity control and removal of acid gas are required simultaneously in a certain space, in general, a humidity control agent such as silica gel is allowed to stand in this space, and a chemical adsorbent for acid gas is allowed to remain static. The method is used.
例えば、美術館や博物館にあっては、展示品の劣化を防止するため、これらの展示ケース内の調湿が求められると共に、これらの展示品に悪影響を及ぼす酢酸ガスなどの酸性ガスの除去が求められるところである。かかる酢酸ガスなどは展示ケース内に貼り込まれるクロスの接着剤などから生じるppbレベルのものであるが展示品劣化の因子としてその速やかな除去が求められる。 For example, in art museums and museums, in order to prevent deterioration of exhibits, humidity control in these display cases is required, and acid gases such as acetic acid gas that adversely affect these exhibits must be removed. It is where it is done. Such acetic acid gas has a ppb level generated from a cloth adhesive or the like stuck in the display case, but its rapid removal is required as a factor of display deterioration.
ここで、こうした展示ケース内に調湿剤と化学吸着剤とをそれぞれ静置させた場合、酸性ガスは調湿剤には物理吸着され化学吸着剤には化学吸着されることとなるが、調湿剤は吸放湿を繰り返すため吸湿時に物理吸着された酸性ガスの成分は放湿時に再び展示ケース内に解き放たれてしまう。このため、このようにした場合、展示ケース内の酸性ガスの濃度を漸減はできるものの、急速に低下させることはできない。また、かかる展示ケース内の空間など、調湿と酸性ガスの除去とが同時に必要とされる空間が狭小である場合には、そこに調湿剤と化学吸着剤とを同時に静置させるスペースを確保し得ない場合もある。調湿剤と化学吸着剤とを単純に混合した場合、静置スペースは減少させることはできるとしても、混ぜられた調湿剤の放湿時にそれに物理吸着された酸性ガスの成分を再び解放させてしまう点は変わらない。熱可塑性樹脂を調湿剤とガス吸着剤と共に混練し成形して構成される調湿吸ガス性成形品として特許文献1に示されるものがあるが、この特許文献1に示されるものも調湿剤と吸着剤とが均一に混ざり合い結びついているわけではなく、両者を単純に混合した場合と変わるものではない。
この発明が解決しようとする主たる問題点は、吸湿特性を利用して酸性ガスを効率的に捕捉しつつ、放湿時に捕捉した酸性ガスを解放させてしまうことがない調湿吸ガス剤、およびこれを利用してなる調湿吸ガス具の提供を目的としている。 The main problem to be solved by the present invention is that the moisture-controlling agent that efficiently captures the acid gas by utilizing the moisture absorption property and does not release the acid gas captured at the time of moisture release, and The object is to provide a humidity-controlled gas-absorbing device using this.
前記課題を達成するために、この発明にあっては、調湿吸ガス剤を、モンモリロナイトを主成分とする粘土鉱物よりなる粉末状をなす調湿材と粉末状をなす酸性ガスの吸着材とを主原料として造粒して得られる多孔質の粒状体の集合物に対し、水分調整してなるものとした。 In order to achieve the above-mentioned object, in the present invention, the moisture-adsorbing agent includes a moisture-conditioning material in the form of a powder made of a clay mineral mainly composed of montmorillonite, and an adsorbent for the acidic gas in the form of a powder. The water content was adjusted for an aggregate of porous granules obtained by granulating as a main raw material.
また、調湿吸ガス具を、前記調湿吸ガス剤を通気性を備えた袋体又は容器に封入してなるものとした。 In addition, the humidity-adjusting and gas-absorbing device is formed by sealing the humidity-adjusting and absorbing agent in a bag or container having air permeability.
この発明にかかる調湿吸ガス剤によれば、含まれる調湿材の吸湿特性を利用して酸性ガスを効率的に捕捉しつつ、この調湿材と一体化された吸着材によって放湿時に捕捉した酸性ガスを解放させてしまうことがなく、この結果、これが静置された空間内の酸性ガスの濃度を急速に減少させることができる。また、この発明にかかる調湿吸ガス具によれば、調湿と酸性ガスの除去が求められる空間内にこれを静置することにより、封入された調湿吸ガス剤によってこの空間内の調湿をしつつこの空間内にある酸性ガスの濃度を急速に減少させることができる。 According to the humidity control gas absorbent according to the present invention, while the acid gas is efficiently captured by utilizing the moisture absorption characteristics of the contained humidity control material, the moisture absorbent is integrated with the humidity control material at the time of moisture release. The trapped acid gas is not released, and as a result, the concentration of the acid gas in the space in which it is placed can be rapidly reduced. In addition, according to the humidity control apparatus according to the present invention, the humidity control device in the space is controlled by the enclosed humidity control gas absorbent by leaving it in a space where humidity control and removal of acid gas are required. The concentration of acid gas in this space can be rapidly reduced while humidifying.
以下、この発明を実施するための最良の形態について説明する。 Hereinafter, the best mode for carrying out the present invention will be described.
この実施の形態にかかる調湿吸ガス剤は、調湿機能と酸性ガスの捕捉吸着機能を備えた多孔質の粒状体の集合物であって、調湿対象となる空間内に静置されて、この空間内の調湿をなすと同時にこの空間内にある酸性ガスを捕捉吸着するものである。 The humidity control gas absorbent according to this embodiment is an aggregate of porous granules having a humidity control function and an acid gas capture and adsorption function, and is placed in a space to be controlled. In addition to adjusting the humidity in this space, the acidic gas in this space is captured and adsorbed.
また、この実施の形態にかかる調湿吸ガス具は、かかる調湿吸ガス剤を通気性を備えた袋体又は容器に封入してなり、調湿対象となる空間内に静置することにより、この空間内の調湿と酸性ガスの除去とを通じてこの空間内にある物品の劣化などを防止するために用いられるものである。 In addition, the humidity control and gas absorption device according to this embodiment is formed by enclosing the humidity control gas absorbent in a bag or container having air permeability and leaving it in the space to be controlled by humidity. It is used to prevent deterioration of articles in the space through humidity control and acid gas removal in the space.
かかる袋体としては、例えば、織物メッシュや不織布などの通気性を備え、かつ、前記粒状体よりも小さい目を持った袋構成材よりなる袋体を用いることができる。また、かかる容器としては、例えば、前記粒状体よりも小さい通気孔を備えた箱状体を用いることができる。 As such a bag, for example, a bag made of a bag constituent material having air permeability such as a woven mesh or a non-woven fabric and having eyes smaller than the granular material can be used. Moreover, as such a container, for example, a box-shaped body having a smaller air hole than the granular body can be used.
調湿吸ガス剤は、調湿材と吸着材とに必要に応じて結合剤を加えて造粒して生成された粒状体の集合物に対し水分調整をして得られる。 The humidity-adjusting gas-absorbing agent is obtained by adjusting the moisture content of the aggregate of granules formed by adding a binder to the humidity-adjusting material and the adsorbent as necessary.
調湿材は、モンモリロナイトを主成分とする粘土鉱物よりなり粉末状をなす。かかる調湿材としては、酸性白土、ベントナイトなどが用いられる。 The humidity control material is made of a clay mineral mainly composed of montmorillonite and is in powder form. As such a humidity control material, acid clay, bentonite or the like is used.
吸着材は、粉末状をなし、酸性ガスを化学吸着するものである。かかる吸着材としては、除去すべき酸性ガスが酢酸ガスである場合、消石灰(水酸化カルシウム)や炭酸カリウムなどが用いられる。 The adsorbent is in a powder form and chemically adsorbs acid gas. As the adsorbent, when the acidic gas to be removed is acetic acid gas, slaked lime (calcium hydroxide) or potassium carbonate is used.
前記結合剤としては、コロイダルシリカなどを用いることができる。 As the binder, colloidal silica or the like can be used.
造粒は、前記粒状体を生成すると共に、生成される粒状体を多孔質構造のものとし、調湿材と吸着材とをできるだけ粒の揃った均一な粒子とし、さらにこれらを偏頗なく混ぜ合わせ一体化させるためになされる。調湿材と吸着材は、造粒に先立ち、あるいは、造粒と同時に混練される。湿式造粒では加水がなされる。造粒は圧縮造粒、撹拌混合造粒、転動造粒、流動層造粒などの周知の方法でなすことができるが、前記の多孔質構造化と両材の粒子の均一化及び混合状態の均質化の観点からは、かかる造粒は、押出造粒によってなすことが最適と認められた。典型的には、かかる押出造粒によって、前記調湿材と吸着材を主原料としてこれらから直径1mm〜3mmで長さ4mm〜8mmの長細い粒状体を生成する。 In granulation, the granule is generated, the generated granule is made of a porous structure, and the humidity control material and the adsorbent are made as uniform particles with as many grains as possible. Made to unite. The humidity control material and the adsorbent are kneaded prior to granulation or simultaneously with granulation. In wet granulation, water is added. Granulation can be carried out by well-known methods such as compression granulation, stirring and mixing granulation, rolling granulation, fluidized bed granulation, etc., but the above-mentioned porous structure and homogenization and mixing state of particles of both materials From the viewpoint of homogenization, it was recognized that the granulation was optimally performed by extrusion granulation. Typically, such extrusion granulation produces long and thin granules having a diameter of 1 mm to 3 mm and a length of 4 mm to 8 mm from the humidity control material and the adsorbent as main raw materials.
各材料は、調湿材40〜90wt%、吸着材10〜60wt%の割合で配合することができるが、調湿性能及びガス吸着性能の双方を十分に満足させる観点からは、調湿材60〜80wt%、吸着材20〜40wt%の割合で配合することが最適と認められた。 Although each material can be mix | blended in the ratio of 40-90 wt% of humidity control materials and 10-60 wt% of adsorbents, from the viewpoint of fully satisfying both humidity control performance and gas adsorption performance, the humidity control material 60 is used. It was recognized that it was optimal to blend in a ratio of ˜80 wt% and adsorbent 20-40 wt%.
調湿吸ガス剤の水分調整は、例えば、調湿対象空間が相対湿度55%に保たれるべき空間である場合には、調湿吸ガス剤がこの空間に調湿吸ガス剤を静置したときにこの空間を相対湿度55%とする吸放湿特性を持つようになされる。より具体的には、かかる吸放湿特性の付与は、典型的には、乾燥させた調湿吸ガス剤に一定量の水分を付与することでなされる。このときに付与すべき水分量は、例えば調湿吸ガス剤に相対湿度55%とする吸放湿特性を持たせる場合には、乾燥させた調湿吸ガス剤(試験用)を相対湿度55%に保たれた空間に吸湿が止まるまで(調湿吸ガス剤の吸湿による重量増加がなくなった状態、以下平衡状態という。)静置し、その静置前(吸湿前)の重量とこの平衡状態での重量との差を求めることで把握することができる。 For example, when the humidity adjustment target space is a space that should be maintained at a relative humidity of 55%, the humidity adjustment gas absorbent keeps the humidity adjustment gas absorbent in this space. In this case, the space has a moisture absorption / release characteristic with a relative humidity of 55%. More specifically, such moisture absorption / release characteristics are typically imparted by imparting a certain amount of moisture to the dried moisture conditioning gas absorbent. The amount of water to be applied at this time is, for example, when the moisture-adsorbing agent has a moisture absorption / release characteristic of 55% relative humidity, and the humidity-adsorbing agent dried (for testing) has a relative humidity of 55%. % Until the moisture absorption stops (the state where the weight increase due to the moisture absorption of the humidity control gas absorbent is ceased, hereinafter referred to as the equilibrium state), and the weight before the standing (before moisture absorption) and this equilibrium. It can be grasped by obtaining the difference from the weight in the state.
このように水分調整された粒状体の集合物、すなわち、調湿吸ガス剤は、気密状態で包装などされ、使用時に開梱されて使用に供される。前記調湿吸ガス具にあっても、気密状態で包装などされ、使用時に開梱されて使用に供される。 The aggregate of granular materials whose moisture has been adjusted in this way, that is, the humidity-adjusting gas-absorbing agent, is packaged in an airtight state, etc., and is unpacked and used for use. Even if it exists in the said humidity control gas absorption tool, it is packaged etc. in an airtight state, is unpacked at the time of use, and is used.
かかる調湿吸ガス剤は、粒状物の集合物であり、かつ、多孔質構造を有することから、高い調湿能力とガス吸着能力を有する。調湿材の吸湿作用によって調湿吸ガス剤の静置された空間内の酸性ガスは粒状物内に取り込まれる。取り込まれた酸性ガス成分は調湿材に物理吸着され、また、吸着材に化学吸着される。調湿材の放湿作用により調湿材に物理吸着されていた酸性ガス成分は解放されるが、造粒によって調湿材と吸着材は偏頗なく一体化されていることから、調湿材と吸着材とを単純に混合した場合と異なり、解放された酸性ガス成分は吸着材に捕捉吸着されて粒状物から抜け出すことがない。すなわち、かかる調湿吸ガス剤によれば、含まれる調湿材の吸湿特性を利用して酸性ガスを効率的に捕捉しつつ、この調湿材と一体化された吸着材によって放湿時に捕捉した酸性ガスを解放させてしまうことがなく、この結果、これが静置された空間内の酸性ガスの濃度を急速に減少させることができる。図1にかかる調湿吸ガス剤の一粒の構造のイメージを模式的に示す。調湿材1と吸着材2は偏頗なく一体化されており、また、かかる調湿吸ガス剤の一粒は多孔質構造を持っている。(図1において孔を符号3で示す。)
Such a humidity control gas-absorbing agent is an aggregate of particulates and has a porous structure, and thus has a high humidity control capability and gas adsorption capability. The acid gas in the space where the humidity adjusting gas-absorbing agent is allowed to stand is taken into the particulate matter by the moisture absorbing action of the humidity adjusting material. The incorporated acidic gas component is physically adsorbed on the humidity control material and chemisorbed on the adsorbent. The acidic gas component physically adsorbed on the humidity control material is released by the moisture release action of the humidity control material, but the humidity control material and the adsorbent are integrated without any deviation by granulation. Unlike the case where the adsorbent is simply mixed, the released acid gas component is captured and adsorbed by the adsorbent and does not escape from the particulate matter. That is, according to such a humidity control gas absorbent, the acidic gas is efficiently captured by utilizing the moisture absorption characteristics of the contained humidity control material, and is captured when the moisture is released by the adsorbent integrated with the humidity control material. As a result, the concentration of the acid gas in the space in which it is placed can be rapidly reduced. The image of the structure of one grain of the humidity adjustment gas absorbent concerning FIG. 1 is shown typically. The
以下の実施例と、比較例1および2を用意し、以下の試験条件の下で試験を行った。 The following examples and comparative examples 1 and 2 were prepared and tested under the following test conditions.
実施例:酸性白土70重量部、消石灰30重量部、結合剤5重量部を造粒して得られた粒状体の集合物
比較例1:粒状の酸性白土70重量部と粒状の消石灰30重量部との混合物
比較例2:シリカゲル70重量部と粒状の消石灰30重量部との混合物
Example: Aggregate of granules obtained by granulating 70 parts by weight of acid clay, 30 parts by weight of slaked lime, and 5 parts by weight of binder Comparative Example 1: 70 parts by weight of granular acid clay and 30 parts by weight of granular slaked lime Comparative Example 2: Mixture of 70 parts by weight of silica gel and 30 parts by weight of granular slaked lime
(試験条件)
実施例、比較例1、比較例2をそれぞれ、酢酸2gを静置させた50Lの密閉容器内に静置し、24時間放置させ酢酸を吸着させた。直径25mm、長さ350mmのガラスカラムに、酢酸を吸着させた実施例、比較例1、比較例2をそれぞれ50mmの長さで充填し、相対湿度20%RHのエアを3.0L/minの通気量で通気させた。通気2時間後と24時間後にそれぞれガス検知管法(下記の表では検知管法と称する。)とイオンクロマトグラフ法(下記の表ではIC法と称する。)によりガラスカラムの下流側の酢酸ガス濃度を測定した。その結果を以下に示す。
Example, Comparative Example 1 and Comparative Example 2 were each left in a 50 L sealed container in which 2 g of acetic acid was allowed to stand and allowed to stand for 24 hours to adsorb acetic acid. A glass column having a diameter of 25 mm and a length of 350 mm was filled with Example, Comparative Example 1 and Comparative Example 2 in which acetic acid was adsorbed in a length of 50 mm, and air having a relative humidity of 20% RH was 3.0 L / min. Aeration was performed with a ventilation amount. After 2 hours and 24 hours of aeration, acetic acid gas on the downstream side of the glass column by the gas detector tube method (referred to as detector tube method in the table below) and ion chromatograph method (referred to as IC method in the table below), respectively. Concentration was measured. The results are shown below.
実施例は、比較例1および比較例2に比べて、時間の経過にかかわらず酢酸ガスの脱離放出量が明らかに少ないことが分かった。 As compared with Comparative Example 1 and Comparative Example 2, it was found that the amount of acetic acid gas desorbed and released was obviously smaller in Examples than in Comparative Examples 1 and 2.
1 調湿材
2 吸着材
3 孔
1
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2289857A3 (en) * | 2009-08-28 | 2011-08-31 | Empa | Moisture and volatile organic matter storing building material and plaster |
JP2014069109A (en) * | 2012-09-28 | 2014-04-21 | Tokai Chemical Industry Co Ltd | Plate-like drier |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61293546A (en) * | 1985-06-21 | 1986-12-24 | Nippon Chem Ind Co Ltd:The | Acidic gas removing agent |
JPH0280696A (en) * | 1988-09-17 | 1990-03-20 | Tokushu Seishi Kk | Neutral paper having moisture-absorbing and-desorbing ability and having excellent gas-adsorbing ability and production thereof |
JPH0389915A (en) * | 1989-08-31 | 1991-04-15 | Toray Ind Inc | Moisture adsorption-desorption material and sheet-like material thereof |
JPH0761480A (en) * | 1993-08-20 | 1995-03-07 | Nippon Soda Co Ltd | Deodorant/desiccant |
JP2002239326A (en) * | 2001-02-15 | 2002-08-27 | National House Industrial Co Ltd | Air cleaner |
JP2005040678A (en) * | 2003-07-24 | 2005-02-17 | Yahashi Kogyo Kk | Humidity conditioning member and porous sintered body used therein |
-
2007
- 2007-05-22 JP JP2007135278A patent/JP2008289955A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61293546A (en) * | 1985-06-21 | 1986-12-24 | Nippon Chem Ind Co Ltd:The | Acidic gas removing agent |
JPH0280696A (en) * | 1988-09-17 | 1990-03-20 | Tokushu Seishi Kk | Neutral paper having moisture-absorbing and-desorbing ability and having excellent gas-adsorbing ability and production thereof |
JPH0389915A (en) * | 1989-08-31 | 1991-04-15 | Toray Ind Inc | Moisture adsorption-desorption material and sheet-like material thereof |
JPH0761480A (en) * | 1993-08-20 | 1995-03-07 | Nippon Soda Co Ltd | Deodorant/desiccant |
JP2002239326A (en) * | 2001-02-15 | 2002-08-27 | National House Industrial Co Ltd | Air cleaner |
JP2005040678A (en) * | 2003-07-24 | 2005-02-17 | Yahashi Kogyo Kk | Humidity conditioning member and porous sintered body used therein |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2289857A3 (en) * | 2009-08-28 | 2011-08-31 | Empa | Moisture and volatile organic matter storing building material and plaster |
JP2014069109A (en) * | 2012-09-28 | 2014-04-21 | Tokai Chemical Industry Co Ltd | Plate-like drier |
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