JP5778991B2 - Gas generator - Google Patents

Gas generator Download PDF

Info

Publication number
JP5778991B2
JP5778991B2 JP2011116998A JP2011116998A JP5778991B2 JP 5778991 B2 JP5778991 B2 JP 5778991B2 JP 2011116998 A JP2011116998 A JP 2011116998A JP 2011116998 A JP2011116998 A JP 2011116998A JP 5778991 B2 JP5778991 B2 JP 5778991B2
Authority
JP
Japan
Prior art keywords
liquid
container
gas
containers
gas generator
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.)
Active
Application number
JP2011116998A
Other languages
Japanese (ja)
Other versions
JP2012246152A (en
Inventor
吉田 真也
真也 吉田
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.)
Earth Chemical Co Ltd
Original Assignee
Earth 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 Earth Chemical Co Ltd filed Critical Earth Chemical Co Ltd
Priority to JP2011116998A priority Critical patent/JP5778991B2/en
Publication of JP2012246152A publication Critical patent/JP2012246152A/en
Application granted granted Critical
Publication of JP5778991B2 publication Critical patent/JP5778991B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Description

本発明は気体発生装置に関し、より詳しくは化学反応によって二酸化塩素や二酸化炭素などの気体を発生させる装置に関する。   The present invention relates to a gas generator, and more particularly to an apparatus for generating a gas such as chlorine dioxide or carbon dioxide by a chemical reaction.

複数の化学物質を混合することによって気体を発生させる装置が知られている。例えば、下記特許文献1,2に記載の装置は除菌や、消臭の作用を有する二酸化塩素ガスを発生させるためのものである。特許文献1に記載の装置はゲル状の安定化二酸化塩素と粒状クエン酸を接触させて二酸化塩素ガスを発生させ、他方、特許文献2に記載の装置は亜塩素酸ナトリウムの粉末と酸性液を接触させて二酸化塩素ガスを発生させる。   An apparatus that generates gas by mixing a plurality of chemical substances is known. For example, the devices described in Patent Documents 1 and 2 below are for generating chlorine dioxide gas having sterilizing and deodorizing functions. The apparatus described in Patent Document 1 generates stabilized chlorine dioxide gas by contacting gelled stabilized chlorine dioxide and granular citric acid, while the apparatus described in Patent Document 2 uses sodium chlorite powder and acidic liquid. Contact to generate chlorine dioxide gas.

特開2009−256141号公報JP 2009-256141 A 特開2009−234887号公報JP 2009-234877 A

ところで、除菌等の用途に用いられる二酸化塩素ガスの他にも、日常生活においては種々の目的のために気体が利用されている。例えば、二酸化炭素は蚊を吸引する作用を有し、蚊をおびき寄せて捕獲するのに利用されている。   Incidentally, in addition to chlorine dioxide gas used for sterilization and the like, gas is used for various purposes in daily life. For example, carbon dioxide has an action of sucking mosquitoes and is used to attract and capture mosquitoes.

従来、液体同士を混合して液−液反応によって気体を発生させる場合、反応性が高いために気体の発生量をコントロールすることが困難であった。上記特許文献1,2に記載の発明にあっては、混合する化学物質をゲル状、粒状又は粉状としたことで、ある程度は気体の発生量のコントロールが可能となった。   Conventionally, when liquids are mixed and gas is generated by a liquid-liquid reaction, it is difficult to control the amount of gas generated due to high reactivity. In the inventions described in Patent Documents 1 and 2, the amount of gas generated can be controlled to some extent by making the chemical substance to be mixed into a gel, granule, or powder.

しかし、特許文献1に記載の装置は、二酸化塩素ガスを発生させるに際して振動を与えて粒状クエン酸をゲル状の安定化二酸化塩素の上面に落下させる必要がある。他方、特許文献2に記載の装置は、亜塩素酸ナトリウムの粉末を収容した袋を開封して当該粉末を容器に入れ、そこに酸性液を注入するタイプであるため、酸性液の注入直後に多量の気体が発生し、その後は短時間のうちに気体の発生量が低下する。   However, the apparatus described in Patent Document 1 needs to drop the granular citric acid onto the upper surface of the gel-like stabilized chlorine dioxide by generating vibration when generating chlorine dioxide gas. On the other hand, the device described in Patent Document 2 is a type in which a bag containing sodium chlorite powder is opened, the powder is placed in a container, and an acidic liquid is injected therein. A large amount of gas is generated, and thereafter the amount of gas generated decreases within a short time.

本発明は上記課題に鑑みてなされたものであり、従来と比較して長期にわたって安定的に気体を生じさせることが可能な気体発生装置を提供することを目的とする。   This invention is made | formed in view of the said subject, and it aims at providing the gas generator which can produce gas stably over a long period of time compared with the past.

本発明に係る気体発生装置は、第1の液体を収容する第1の容器と、第2の液体を収容する第2の容器と、第1の液体と接触する第1の吸液部、第2の液体と接触する第2の吸液部、及び、第1の液体と第2の液体の化学反応による気体を生じさせる蒸散部を有する吸液材とを備える。   A gas generator according to the present invention includes a first container that contains a first liquid, a second container that contains a second liquid, a first liquid-absorbing part that contacts the first liquid, A second liquid-absorbing part that comes into contact with the second liquid, and a liquid-absorbing material having a transpiration part that generates a gas by a chemical reaction between the first liquid and the second liquid.

上記気体発生装置においては、第1の吸液部及び第2の吸液部を通じて第1の液体及び第2の液体が蒸散部に染み出すようにして供給される。このため、振動等を与えなくても蒸散部において第1の液体及び第2の液体による液−液反応が徐々に進行し、十分に安定的に且つ長期にわたって気体を発生させることができる。気体が安定的に発生することで、気体を発生させるべき環境において発生気体の濃度を所望の範囲に十分にコントロールできる。   In the gas generator, the first liquid and the second liquid are supplied to the transpiration unit through the first liquid absorption unit and the second liquid absorption unit. For this reason, even if vibration etc. are not given, the liquid-liquid reaction by the 1st liquid and the 2nd liquid advances gradually in a transpiration | evaporation part, and can generate | occur | produce gas sufficiently stably over a long period of time. Since the gas is stably generated, the concentration of the generated gas can be sufficiently controlled within a desired range in an environment where the gas is to be generated.

上記気体発生装置の発生気体は二酸化塩素又は二酸化炭素とすることができる。発生気体が二酸化塩素である場合、第1の液体は亜塩素酸塩の水溶液とし、一方、第2の液体は酸性物質の水溶液とすればよい。発生気体が二酸化炭素である場合、第1の液体は炭酸水素ナトリウムの水溶液とし、一方、第2の液体は酸性物質の水溶液とすればよい。   The gas generated by the gas generator can be chlorine dioxide or carbon dioxide. When the generated gas is chlorine dioxide, the first liquid may be an aqueous solution of chlorite, while the second liquid may be an aqueous solution of an acidic substance. When the generated gas is carbon dioxide, the first liquid may be an aqueous solution of sodium hydrogen carbonate, while the second liquid may be an aqueous solution of an acidic substance.

上記吸液材は気孔率が20〜80%の多孔性材料からなることが好ましい。かかる構成を採用することにより、吸液部において十分な吸液性を確保できるとともに第1の液体と第2の液体の化学反応によって蒸散部に塩などの反応生成物が蓄積しても目詰まりを十分に防止できる。なお、本発明でいう「気孔率」は、下記式によって算出される値を意味する。

Figure 0005778991

式中、W1は水を目一杯吸収させた後の吸液材の質量(g);W0は水を吸収させる前の吸液材の質量(g);ρは水の密度(g/cm);Vは吸液材の見かけ体積(cm)をそれぞれ示す。 The liquid absorbent material is preferably made of a porous material having a porosity of 20 to 80%. By adopting such a configuration, sufficient liquid absorbability can be secured in the liquid absorption part, and clogging is caused even if a reaction product such as salt accumulates in the evaporation part due to a chemical reaction between the first liquid and the second liquid. Can be sufficiently prevented. The “porosity” in the present invention means a value calculated by the following formula.
Figure 0005778991

In the formula, W1 is the mass (g) of the liquid-absorbing material after fully absorbing water; W0 is the mass (g) of the liquid-absorbing material before absorbing water; ρ is the density of water (g / cm 3 V represents the apparent volume (cm 3 ) of the liquid-absorbing material.

上記気体発生装置の態様は、いわゆる正立型又は倒立型のいずれであってもよい。正立型の気体発生装置は、第1の容器及び第2の容器を保持する容器保持体を更に備え、第1の容器及び第2の容器は吸液材が挿入される開口を上方にそれぞれ有し、蒸散部が第1の容器及び第2の容器の上方に配置された態様とすることができる。倒立型の気体発生装置は、第1の容器及び第2の容器を保持する容器保持体を更に備え、第1の容器及び第2の容器は液体排出用の開口を下方にそれぞれ有し、蒸散部が第1の容器及び第2の容器の下方に配置された態様とすることができる。   The mode of the gas generator may be either a so-called upright type or an inverted type. The upright gas generator further includes a container holding body for holding the first container and the second container, and the first container and the second container respectively have openings into which the liquid absorbing material is inserted upward. And the transpiration unit may be arranged above the first container and the second container. The inverted gas generator further includes a container holding body for holding the first container and the second container, and the first container and the second container each have an opening for discharging the liquid below, It can be set as the aspect by which the part was arrange | positioned under the 1st container and the 2nd container.

本発明によれば、従来と比較して長期にわたって安定的に気体を生じさせることができる。   According to the present invention, it is possible to stably generate gas over a long period of time compared to the prior art.

本発明に係る気体発生装置の第一実施形態(正立型)を示す斜視図である。1 is a perspective view showing a first embodiment (upright type) of a gas generator according to the present invention. 図1に示す気体発生装置の構成を示す分解図である。It is an exploded view which shows the structure of the gas generator shown in FIG. 本発明に係る気体発生装置の第二実施形態(倒立型)を示す斜視図である。It is a perspective view which shows 2nd embodiment (inverted type) of the gas generator which concerns on this invention. 図3に示す気体発生装置の構成を示す分解図である。It is an exploded view which shows the structure of the gas generator shown in FIG. 本発明に係る気体発生装置に適用可能な容器の他の態様を示す斜視図である。It is a perspective view which shows the other aspect of the container applicable to the gas generator which concerns on this invention. 実施例及び比較例の結果を示すグラフである。It is a graph which shows the result of an Example and a comparative example.

以下、本発明の好適な実施形態について図面を参照しながら説明する。なお、本発明は以下の実施形態に限定されるものではない。   Preferred embodiments of the present invention will be described below with reference to the drawings. In addition, this invention is not limited to the following embodiment.

<第一実施形態>
図1,2に示す気体発生装置10は、第1及び第2の液体をそれぞれ収容する第1及び第2の容器1,2と、第1及び第2の吸液部3a,3b及び気体を発生させる化学反応の反応場をなす蒸散部3cを有する吸液材3と、容器1,2を保持する容器保持体5とを備える。気体発生装置10は、いわゆる正立型であり、蒸散部3cが容器1,2の上方に配置されている。
<First embodiment>
The gas generator 10 shown in FIGS. 1 and 2 includes first and second containers 1 and 2 that respectively contain first and second liquids, first and second liquid-absorbing portions 3a and 3b, and gas. The liquid-absorbing material 3 having a transpiration portion 3c that forms a reaction field for a chemical reaction to be generated, and a container holder 5 that holds the containers 1 and 2 are provided. The gas generator 10 is a so-called upright type, and the transpiration unit 3 c is disposed above the containers 1 and 2.

図2に示す容器1,2は、第1及び第2の液体をそれぞれ収容するためのものであり、容器保持体5内に並ぶように配置されている。容器1,2のそれぞれの内容積は、発生させる気体の種類や使用場所などによって適宜設定すればよい。容器1,2に材質としては、液体が漏れないものであれば特に制限はなく、プラスチック、紙、金属、セラミック又はガラス等のいずれであってもよい。ここでは容器1,2として円筒状のものを挙げたが、容器1,2の形状はこれに限定されない。   The containers 1 and 2 shown in FIG. 2 are for storing the first and second liquids, respectively, and are arranged in the container holder 5. What is necessary is just to set suitably each internal volume of the containers 1 and 2 according to the kind of gas to be generated, a place of use, etc. The material for the containers 1 and 2 is not particularly limited as long as the liquid does not leak, and may be plastic, paper, metal, ceramic, glass, or the like. Here, although the cylindrical thing was mentioned as the containers 1 and 2, the shape of the containers 1 and 2 is not limited to this.

容器1,2は、吸液材3の吸液部3a,3bをそれぞれ挿入するための開口1a,2aを上方に有する。開口1a,2aはキャップ1b,2bでそれぞれ塞ぐことが可能な構成とすることが好ましい(図2参照)。かかる構成を採用することにより、気体発生装置10の製造後、キャップ1b,2bを装着した状態で搬送等を行うことができる。   The containers 1 and 2 have openings 1a and 2a for inserting the liquid absorbing portions 3a and 3b of the liquid absorbing material 3, respectively. The openings 1a and 2a are preferably configured to be closed by caps 1b and 2b, respectively (see FIG. 2). By adopting such a configuration, after the gas generator 10 is manufactured, conveyance or the like can be performed with the caps 1b and 2b attached.

容器1,2にそれぞれ収容する1及び第2の液体は、発生させる気体に応じて適宜選択すればよい。発生させる気体としては、二酸化塩素又は二酸化炭素が挙げられる。   What is necessary is just to select suitably the 1st and 2nd liquid each accommodated in the containers 1 and 2 according to the gas to generate | occur | produce. Examples of the gas to be generated include chlorine dioxide and carbon dioxide.

二酸化塩素を発生させる場合、第1の液体は亜塩素酸塩の水溶液とし、一方、第2の液体は酸性物質の水溶液とすればよい。亜塩素酸塩の水溶液(第1の水溶液)の具体例としては、亜塩素酸のアルカリ金属塩(例えば亜塩素酸ナトリウム)の水溶液アルカリ土類金属塩(例えば亜塩素酸カルシウム)の水溶液等が挙げられる。酸性物質の水溶液(第2の水溶液)の具体例としては、クエン酸水溶液、リンゴ酸水溶液、酒石酸、リン酸、アスコルビン酸等が挙げられ、これらのうち取扱いの容易性及び安全性の観点からクエン酸水溶液、リンゴ酸水溶液、酒石酸などの食用有機酸の水溶液がより好ましい。   When generating chlorine dioxide, the first liquid may be an aqueous solution of chlorite, while the second liquid may be an aqueous solution of an acidic substance. Specific examples of the aqueous solution of chlorite (first aqueous solution) include an aqueous solution of an alkaline metal salt of chlorite (eg, sodium chlorite), an alkaline earth metal salt (eg, calcium chlorite), and the like. Can be mentioned. Specific examples of the aqueous solution of the acidic substance (second aqueous solution) include citric acid aqueous solution, malic acid aqueous solution, tartaric acid, phosphoric acid, ascorbic acid and the like. Among these, from the viewpoint of ease of handling and safety, An aqueous solution of an edible organic acid such as an acid aqueous solution, malic acid aqueous solution or tartaric acid is more preferable.

亜塩素酸塩の水溶液及び酸性物質の水溶液の濃度は、発生させる二酸化塩素の濃度や持続時間等に応じて適宜設定すればよい。気体発生装置10が例えば家庭や病院などで使用されるものである場合、亜塩素酸塩の水溶液の濃度は0.5〜15質量%程度とすればよく、酸性物質の水溶液の濃度も0.5〜15質量%程度とすればよい。   What is necessary is just to set suitably the density | concentration of the aqueous solution of a chlorite, and the aqueous solution of an acidic substance according to the density | concentration, duration, etc. of the chlorine dioxide to generate | occur | produce. When the gas generator 10 is used, for example, at home or in a hospital, the concentration of the aqueous solution of chlorite may be about 0.5 to 15% by mass, and the concentration of the aqueous solution of acidic substance is also 0.1. What is necessary is just to set it as about 5-15 mass%.

二酸化炭素を発生させる場合、第1の液体は炭酸水素ナトリウムの水溶液とし、一方、第2の液体は酸性物質の水溶液とすればよい。酸性物質の水溶液(第2の水溶液)としては、上述の二酸化塩素を発生させる場合と同様のものを採用すればよい。炭酸水素ナトリウムの水溶液及び酸性物質の水溶液の濃度は、発生させる二酸化炭素の濃度や持続時間等に応じて適宜設定すればよい。気体発生装置10が例えば家庭や病院などで使用されるものである場合、炭酸水素ナトリウムの水溶液の濃度は0.5〜10質量%程度とすればよく、酸性物質の水溶液の濃度も0.5〜10質量%程度とすればよい。   When generating carbon dioxide, the first liquid may be an aqueous solution of sodium bicarbonate, while the second liquid may be an aqueous solution of an acidic substance. As the aqueous solution of the acidic substance (second aqueous solution), the same solution as that used for generating chlorine dioxide may be adopted. What is necessary is just to set suitably the density | concentration of the aqueous solution of sodium hydrogencarbonate, and the aqueous solution of an acidic substance according to the density | concentration, duration, etc. of the carbon dioxide to generate | occur | produce. When the gas generator 10 is used, for example, at home or in a hospital, the concentration of the aqueous solution of sodium bicarbonate may be about 0.5 to 10% by mass, and the concentration of the aqueous solution of acidic substance is also 0.5. What is necessary is just about 10 mass%.

吸液材3においては、吸液部3a,3bが容器1,2からそれぞれ液体を吸い上げて蒸散部3cに供給する役割を担うとともに、蒸散部3cが第1及び第2の液体による化学反応の場としての役割を担う。図2に示すように、吸液部3a,3bは平板状の蒸散部3cの一方の面(下面)から当該面の法線方向に延びており、容器1,2の開口1a,2aから挿入されて底面1c,2cにまで至る程度の長さを有する。なお、図1,2に示すように、蒸散部3cを保護するためのフレーム4(例えば、プラスチック製)を蒸散部3cの周縁部に設けてもよい。   In the liquid absorbing material 3, the liquid absorbing portions 3a and 3b serve to suck up the liquid from the containers 1 and 2 and supply the liquid to the transpiration portion 3c, respectively, and the transpiration portion 3c performs the chemical reaction by the first and second liquids. Play a role as a place. As shown in FIG. 2, the liquid absorbing parts 3a, 3b extend from one surface (lower surface) of the flat plate-like transpiration unit 3c in the normal direction of the surface, and are inserted from the openings 1a, 2a of the containers 1, 2. And has a length that reaches the bottom surfaces 1c and 2c. As shown in FIGS. 1 and 2, a frame 4 (for example, made of plastic) for protecting the transpiration portion 3 c may be provided on the peripheral portion of the transpiration portion 3 c.

吸液材3を構成する吸液部3a,3b及び蒸散部3cは同一の材質からなるものであっても、互いに異なる材質であってもよい。更に第1及び第2の液体の特性(例えば、粘度等)に応じて吸液部3a及び吸液部3bの材質を互いに異なるものとしてもよい。   The liquid absorbing parts 3a, 3b and the transpiration part 3c constituting the liquid absorbing material 3 may be made of the same material or different materials. Furthermore, the material of the liquid absorbing part 3a and the liquid absorbing part 3b may be different from each other in accordance with the characteristics (for example, viscosity) of the first and second liquids.

吸液部3a,3bの材質としては、毛細管現象によって容器1,2から液体をそれぞれ吸い上げて二種類の液体が蒸散部3cに染み出すように供給できるものであれば特に制限はなく、樹脂、パルプ等の有機材料やガラス等の無機材料の多孔性材料を用いることができる。多孔性材料の好適例としては、パルプもしくは樹脂材料からなる不織布が挙がられる。樹脂材料はポリエチレンテレフタレート(PET)、アクリル樹脂(PA)、ポリプロピレン(PP)、ポリエチレン(PE)から選ばれる1種を単独で用いてもよく2種以上を併用してもよい。   The material of the liquid absorbing parts 3a and 3b is not particularly limited as long as the liquid can be sucked up from the containers 1 and 2 by capillarity so that two kinds of liquid can be supplied to the transpiration part 3c. A porous material such as an organic material such as pulp or an inorganic material such as glass can be used. A preferred example of the porous material is a nonwoven fabric made of pulp or resin material. As the resin material, one kind selected from polyethylene terephthalate (PET), acrylic resin (PA), polypropylene (PP) and polyethylene (PE) may be used alone, or two or more kinds may be used in combination.

吸液部3a,3bはそれぞれ複数の材質によって構成されてもよい。例えば吸液部3a,3bは、パルプを主原料としバインダーで接着させたものであって、表面の強度、保形性のために表裏面にティッシュ状のパルプ材、不織布などを貼った構成としてもよい。また、吸液部3a,3bにそれぞれ第1及び第2の液体を保持させておくことで、使用開始時と同時に、保持された液体が蒸散部3cにそれぞれ供給されて短時間のうちに蒸散部3cにおいて化学反応が生じるようにしてもよい。   The liquid absorbing parts 3a and 3b may each be made of a plurality of materials. For example, the liquid-absorbing parts 3a and 3b are made of pulp as a main raw material and bonded with a binder, and have a structure in which tissue-like pulp materials, non-woven fabrics, etc. are pasted on the front and back surfaces for surface strength and shape retention. Also good. Also, by holding the first and second liquids in the liquid absorption parts 3a and 3b, respectively, the held liquid is supplied to the transpiration part 3c at the same time as the start of use, and transpiration is achieved in a short time. A chemical reaction may occur in the portion 3c.

吸液部3a,3bをそれぞれ構成する多孔性材料の気孔率、密度又は長手方向に垂直な断面のサイズといったパラメータは、液体の粘度や容器1,2の高さ等の諸条件により適宜設定すればよい。これらのパラメータの数値範囲は、容器1,2から液体を効率的に吸い上げて安定的に蒸散部3cに液体を供給する観点から、以下の程度とすることが好ましい。   Parameters such as the porosity, density, or size of the cross section perpendicular to the longitudinal direction of the porous material constituting each of the liquid absorbing portions 3a and 3b are appropriately set according to various conditions such as the viscosity of the liquid and the height of the containers 1 and 2. That's fine. The numerical ranges of these parameters are preferably set to the following levels from the viewpoint of efficiently sucking the liquid from the containers 1 and 2 and stably supplying the liquid to the transpiration unit 3c.

すなわち、吸液部3a,3bの気孔率は好ましくは20〜80%であり、より好ましくは30〜80%である。吸液部3a,3bの密度は、好ましくは0.15〜0.4g/cmである。吸液部3a,3bの断面サイズは、好ましくは3〜300mmであり、より好ましくは12〜120mmである。なお、吸液部3a,3bの断面形状は円形に限られず、矩形、楕円形又は多角形等であってもよい。 That is, the porosity of the liquid absorption parts 3a and 3b is preferably 20 to 80%, more preferably 30 to 80%. The density of the liquid absorbing parts 3a and 3b is preferably 0.15 to 0.4 g / cm 3 . Liquid absorbing portion 3a, the cross-sectional size of 3b is preferably 3~300Mm 2, more preferably 12~120mm 2. In addition, the cross-sectional shape of the liquid absorption parts 3a and 3b is not limited to a circle, and may be a rectangle, an ellipse, a polygon, or the like.

蒸散部3cの材質としては、上述の吸液部3a,3bと同様のものを採用することができる。二種類の液体の化学反応によって蒸散部3cに反応生成物が蓄積しても目詰まりが生じないようにする観点から、蒸散部3cの気孔率は好ましくは20〜80%であり、より好ましくは30〜80%である。同様の観点から、蒸散部3cの目付けは好ましくは200〜2000g/mであり、より好ましくは400〜1600g/mであり、厚さは好ましくは2〜20mmであり、より好ましくは2〜16mmである。 As a material of the transpiration | evaporation part 3c, the thing similar to the above-mentioned liquid absorption parts 3a and 3b is employable. From the viewpoint of preventing clogging even if a reaction product accumulates in the transpiration unit 3c by chemical reaction of two kinds of liquids, the porosity of the transpiration unit 3c is preferably 20 to 80%, more preferably. 30 to 80%. From the same viewpoint, the basis weight of the transpiration portion 3c is preferably 200 to 2000 g / m 2 , more preferably 400 to 1600 g / m 2 , and the thickness is preferably 2 to 20 mm, more preferably 2 to 2 mm. 16 mm.

なお、蒸散部3cは、容器1,2の開口1a,2aに挿入された状態の吸液部3a,3bから脱着自在な構成としてもよい。かかる構成を採用することで、蒸散部3cにおける反応生成物の蓄積が顕著となった場合に新たな蒸散部3cへの交換が可能となる。   The evaporating part 3c may be configured to be detachable from the liquid absorbing parts 3a and 3b inserted into the openings 1a and 2a of the containers 1 and 2. By adopting such a configuration, when the accumulation of the reaction product in the transpiration unit 3c becomes significant, it can be replaced with a new transpiration unit 3c.

容器保持体5は、容器1,2を一体的に保持するためのものである。図2に示すように、容器保持体5は容器1,2の外面の形状に応じた形状を有しており、容器1,2を収容した際に容器1,2の位置ズレが生じないようになっている。   The container holder 5 is for holding the containers 1 and 2 integrally. As shown in FIG. 2, the container holding body 5 has a shape corresponding to the shape of the outer surface of the containers 1 and 2 so that the containers 1 and 2 are not displaced when the containers 1 and 2 are accommodated. It has become.

気体発生装置10によれば、容器1,2にそれぞれ収容された液体が吸液部3a及び吸液部3bを通じて蒸散部3cに染み出すようにして供給されることで、十分に安定的に且つ長期にわたって蒸散部3cにおいて気体を発生させることができる。   According to the gas generator 10, the liquids stored in the containers 1 and 2 are supplied so as to ooze out to the transpiration unit 3c through the liquid absorption part 3a and the liquid absorption part 3b, so that the liquid generator 10 is sufficiently stable and A gas can be generated in the transpiration | evaporation part 3c over a long period of time.

<第二実施形態>
図3,4に示す気体発生装置20は、第1及び第2の液体をそれぞれ収容する第1及び第2の容器11,12と、吸液材13と、容器11,12を保持する容器保持体15とを備える。気体発生装置20は、いわゆる倒立型であり、吸液材13が容器11,12の下方に配置されている。
<Second embodiment>
The gas generator 20 shown in FIGS. 3 and 4 includes first and second containers 11 and 12 that store first and second liquids, a liquid absorbing material 13, and a container holding that holds the containers 11 and 12, respectively. And a body 15. The gas generator 20 is a so-called inverted type, and the liquid absorbing material 13 is disposed below the containers 11 and 12.

容器11,12は、第1及び第2の液体をそれぞれ収容するためのものであり、容器保持体15上に並ぶように配置されている。容器11,12のそれぞれの内容積は、発生させる気体の種類や使用場所などによって適宜設定すればよい。容器11,12に材質としては、液体が漏れないものであれば特に制限はなく、プラスチック、紙、金属、セラミック又はガラス等のいずれであってもよい。ここでは容器11,12として半球を更に半分に割ったような形状のものを挙げたが、容器11,12の形状はこれに限定されない。   The containers 11 and 12 are for containing the first and second liquids, respectively, and are arranged on the container holding body 15. The internal volume of each of the containers 11 and 12 may be set as appropriate depending on the type of gas to be generated and the place of use. The material for the containers 11 and 12 is not particularly limited as long as the liquid does not leak, and may be plastic, paper, metal, ceramic, glass, or the like. Although the container 11 and 12 have a shape in which the hemisphere is further divided into half, the shape of the containers 11 and 12 is not limited to this.

容器11,12は、収容している液を排出して吸液材13に染み込ませるための開口11a,12aを下方に有する。開口11a,12aはキャップ11b,12bでそれぞれ塞ぐことが可能な構成とすることが好ましい(図4参照)。かかる構成を採用することにより、気体発生装置20の製造後、キャップ11b,12bを装着した状態で搬送等を行うことができる。   The containers 11 and 12 have openings 11a and 12a on the lower side for discharging the contained liquid and allowing the liquid absorbing material 13 to penetrate. The openings 11a and 12a are preferably configured to be closed by caps 11b and 12b, respectively (see FIG. 4). By adopting such a configuration, after the gas generator 20 is manufactured, conveyance or the like can be performed with the caps 11b and 12b attached.

容器11,12にそれぞれ収容する1及び第2の液体は、発生させる気体に応じて適宜選択すればよい。発生させる気体としては、上述の第一実施形態と同様、二酸化塩素又は二酸化炭素が挙げられ、第1及び第2の液体も上述の第一実施形態と同様のものを採用できる。   What is necessary is just to select suitably the 1st and 2nd liquid accommodated in the containers 11 and 12 according to the gas to generate | occur | produce, respectively. Examples of the gas to be generated include chlorine dioxide and carbon dioxide as in the first embodiment described above, and the first and second liquids may be the same as those in the first embodiment described above.

吸液材13は、平板状の形状を有し、容器11,12の開口11a,12aを同時に覆うように配置されている。本実施形態においては、図4においてそれぞれ破線で囲った領域13a,13b及び領域13cが二つの吸液部及び蒸散部に相当する。すなわち、吸液材13における領域13a,13bは、容器11,12の開口11a,12aにそれぞれ対向する領域であり、領域13cは二種類の液体が混ざり合って反応が生じる領域である。   The liquid absorbing material 13 has a flat plate shape and is disposed so as to simultaneously cover the openings 11 a and 12 a of the containers 11 and 12. In the present embodiment, the regions 13a, 13b and the region 13c surrounded by broken lines in FIG. 4 correspond to the two liquid absorption parts and the transpiration part, respectively. That is, the regions 13a and 13b in the liquid absorbing material 13 are regions facing the openings 11a and 12a of the containers 11 and 12, respectively, and the region 13c is a region in which two kinds of liquids are mixed to cause a reaction.

吸液材13は、気液の交換が可能な材質からなる。ここでいう「気液の交換が可能な材質」とは、容器11,12内の液体が吸液材13にそれぞれ浸透して容器11,12の外部に排出されるとともに、容器11,12の外部から吸液材13に浸透した空気等の気体が容器11,12にそれぞれ導入され、容器11,12内が過度に負圧になることを抑制可能な材質を意味する。かかる材質の具体例としては、上述の第一実施形態における吸液材3と同様の材質が挙げられ、これらのなかでも、PET又はPAを用いた多孔性材料を採用することが好ましい。   The liquid absorbing material 13 is made of a material that can exchange gas and liquid. The “material that can exchange gas and liquid” here means that the liquid in the containers 11 and 12 penetrates the liquid absorbing material 13 and is discharged to the outside of the containers 11 and 12. It means a material capable of suppressing gas inside the containers 11 and 12 from being introduced with gas such as air that has penetrated into the liquid absorbing material 13 from the outside and excessively negative pressure inside the containers 11 and 12. Specific examples of such a material include the same material as the liquid-absorbing material 3 in the first embodiment described above, and among these, it is preferable to employ a porous material using PET or PA.

吸液材13を構成する多孔性材料の気孔率や目付け、厚さ等は、液体の粘度や容器11,12の内容積等の諸条件により適宜設定すればよい。開口11a,12aから液体が流れ出るのを防止するとともに吸液材13において化学反応を十分に進行せしめる観点から、吸液材13の気孔率は好ましくは20〜80%であり、より好ましくは30〜80%である。かかる観点及び二種類の液体の化学反応によって領域13cに反応生成物が蓄積しても目詰まりが生じないようにする観点から、吸液材13の目付けは好ましくは200〜2000g/mであり、より好ましくは400〜1600g/mであり、厚さは好ましくは2〜20mmであり、より好ましくは2〜16mmである。なお、吸液材13における領域13cの反応生成物の蓄積が顕著となった場合に新たな吸液材13に交換してもよい。 What is necessary is just to set suitably the porosity of the porous material which comprises the liquid absorbing material 13, a fabric weight, thickness, etc. according to various conditions, such as the viscosity of a liquid, and the internal volume of the containers 11 and 12. From the viewpoint of preventing the liquid from flowing out from the openings 11a and 12a and allowing the chemical reaction to sufficiently proceed in the liquid absorbing material 13, the porosity of the liquid absorbing material 13 is preferably 20 to 80%, more preferably 30 to 30%. 80%. From this viewpoint and the viewpoint of preventing clogging even if reaction products accumulate in the region 13c due to the chemical reaction of two kinds of liquids, the basis weight of the liquid absorbing material 13 is preferably 200 to 2000 g / m 2 . More preferably, it is 400-1600 g / m < 2 >, and thickness is preferably 2-20 mm, More preferably, it is 2-16 mm. In addition, when accumulation of reaction products in the region 13c in the liquid absorbing material 13 becomes significant, the liquid absorbing material 13 may be replaced with a new one.

吸液材13は、全体が同一の材質からなり略均一な物性を有するものであってもよく、あるいは、特定の領域(領域13a、領域13b又は領域13c)について他の領域と異なる材質を配置したり異なる気孔率や厚さに設定したりしてもよい。例えば、吸液材13の一方面に容器11,12の開口11a,12aの形状に応じた隆起部を二つ設け、これらの隆起部に容器11,12の開口11a,12aを嵌め込むことができるようにしてもよい。   The liquid absorbing material 13 may be made of the same material as a whole and have substantially uniform physical properties, or a specific region (region 13a, region 13b or region 13c) may be formed of a material different from other regions. Or may be set to a different porosity or thickness. For example, two raised portions corresponding to the shapes of the openings 11a and 12a of the containers 11 and 12 are provided on one surface of the liquid absorbing material 13, and the openings 11a and 12a of the containers 11 and 12 are fitted into these raised portions. You may be able to do it.

容器保持体15は、容器11,12及び吸液材13を一体的に保持するとともに、スタンドとしての役割を担うものである。容器保持体15は容器11,12の底部の形状及び吸液材13の形状に応じた形状を有する保持部15aと、その下部に設けられたスタンド部15bとによって構成される。保持部15a上に吸液材13及び容器11,12を配置することによってこれらの位置ズレが生じないようになっている。保持部15aには複数の貫通孔15cが形成されており、これらを通じて外部に気体が放出される。   The container holding body 15 integrally holds the containers 11 and 12 and the liquid absorbing material 13 and plays a role as a stand. The container holding body 15 includes a holding portion 15a having a shape corresponding to the shape of the bottom of the containers 11 and 12 and the shape of the liquid absorbing material 13, and a stand portion 15b provided below the holding portion 15a. By disposing the liquid absorbing material 13 and the containers 11 and 12 on the holding portion 15a, these positional deviations do not occur. A plurality of through holes 15c are formed in the holding portion 15a, and gas is released to the outside through these.

気体発生装置20によれば、容器11,12にそれぞれ収容された液体が吸液材13に染み出すようにして供給されることで、十分に安定的に且つ長期にわたって吸液材13(特に領域13c)において気体を発生させることができる。   According to the gas generator 20, the liquid stored in the containers 11 and 12 is supplied so as to ooze into the liquid absorbing material 13, so that the liquid absorbing material 13 (particularly the region) is sufficiently stable and long-term. A gas can be generated in 13c).

以上、本発明の好適な実施形態について詳細に説明したが、本発明は上記実施形態に限定されるものではない。上記第一実施形態においては平板状の蒸散部3cを例示したが、反応場を十分に確保できる態様であれば蒸散部3cの形状は特に制限はない。例えば、棒状の多孔性材料を逆U字状に加工し、両端から上方に延びる部分を容器1,2内にそれぞれ挿入して吸液部とし、横方向に延びる部分を蒸散部としてもよい。   The preferred embodiment of the present invention has been described in detail above, but the present invention is not limited to the above embodiment. In the first embodiment, the flat plate-shaped transpiration unit 3c is exemplified, but the shape of the transpiration unit 3c is not particularly limited as long as the reaction field can be sufficiently secured. For example, a rod-shaped porous material may be processed into an inverted U shape, and the portions extending upward from both ends may be inserted into the containers 1 and 2 to form a liquid absorbing portion, and the portion extending in the lateral direction may be a transpiration portion.

また、上記第一実施形態に係る気体発生装置10は容器保持体5を備える構成としたが、容器1,2を一体的に保持する機能を吸液材3又は保護フレーム4に具備させた場合には容器保持体5を採用しなくてもよい。   Moreover, although the gas generator 10 which concerns on said 1st embodiment set it as the structure provided with the container holding body 5, when the liquid absorbing material 3 or the protective frame 4 was equipped with the function to hold | maintain the containers 1 and 2 integrally, The container holder 5 may not be used.

更に、二つの容器(第1の容器及び第2の容器)は別々のものでなくてもよく、例えば、一つの容器内を仕切ることによってこの容器内に第1の容器及び第2の容器を画成してもよい。図5に示す第1の容器21及び第2の容器22は、装置本体25をなす容器の内部を仕切り板25aで仕切ることによって画成されたものである。図5に示す状態の装置本体25の上方に蒸散部を配置することで正立型の気体発生装置を構成できる。この場合も容器保持体を採用しなくてもよい。図5に示す状態から上下を逆さにして、装置本体25の下方に吸液材及び容器保持体を配置することで倒立型の気体発生装置を構成できる。   Further, the two containers (the first container and the second container) do not have to be separate. For example, the first container and the second container are placed in the container by partitioning the inside of the container. It may be defined. The first container 21 and the second container 22 shown in FIG. 5 are defined by partitioning the inside of the container constituting the apparatus main body 25 with a partition plate 25a. An erecting gas generator can be configured by disposing the transpiration unit above the apparatus main body 25 in the state shown in FIG. Also in this case, the container holder may not be used. An inverted gas generator can be configured by inverting the top and bottom from the state shown in FIG.

以下、本発明について実施例及び比較例によって更に詳しく説明するが、本発明は以下の実施例に限定されるものではない。   EXAMPLES Hereinafter, although an Example and a comparative example demonstrate this invention further in detail, this invention is not limited to a following example.

(実施例1)
図1に示す気体発生装置と同様の構成を有する装置を試作した。一方の容器に亜塩素酸ナトリウム水溶液(濃度13.4質量%、100mL)を入れ、他方の容器にクエン酸水溶液(濃度7.5質量%、100mL)を入れた。吸液材として、PPとPEの複合材料からなる吸液部(2本)と、パルプ製の蒸散紙からなる蒸散部とによって構成された部材を準備した。上記複合材料は直径8mm、気孔率70%であった。上記蒸散紙はハトシートXCA(商品名、王子キノクロス株式会社製)であり、厚さ12mm、目付量1200g/mであった。
Example 1
An apparatus having the same configuration as that of the gas generator shown in FIG. A sodium chlorite aqueous solution (concentration 13.4% by mass, 100 mL) was placed in one container, and a citric acid aqueous solution (concentration 7.5% by mass, 100 mL) was placed in the other container. As a liquid absorbing material, a member constituted by a liquid absorbing part (two) made of a composite material of PP and PE and a transpiration part made of a transpiration paper made of pulp was prepared. The composite material had a diameter of 8 mm and a porosity of 70%. The transpiration paper was pigeon sheet XCA (trade name, manufactured by Oji Kinocross Co., Ltd.), and had a thickness of 12 mm and a basis weight of 1200 g / m 2 .

2つの容器に亜塩素酸ナトリウム及びクエン酸水溶液をそれぞれ収容した後、2つの容器のそれぞれの開口に吸液部を挿入した。その後、この装置を温度約25℃、湿度なりゆき、無風の条件下で保存し、所定の日数経過ごとに二酸化塩素ガスの濃度を測定した。二酸化塩素ガスの濃度は、内容積4Lのデシケータ内に当該装置をその都度収容し、一定の時間静置させた後、デシケータ内の空気をGASTEC(登録商標)GV−100及び気体検知管(No.8H、23M、23L、株式会社ガステック製)を用いて測定した。なお、デシケータ内には当該装置とともに小型ファンを収容し、濃度測定に先立って小型ファンによってデシケータ内の空気を3分間にわたって対流させた。   After the sodium chlorite and the citric acid aqueous solution were respectively stored in the two containers, the liquid absorption part was inserted into each opening of the two containers. Thereafter, this apparatus was stored under conditions of a temperature of about 25 ° C., humidity, and no wind, and the concentration of chlorine dioxide gas was measured every predetermined number of days. The concentration of chlorine dioxide gas is determined by accommodating the device in a 4 L internal volume desiccator each time and allowing it to stand for a certain period of time, and then letting the air in the desiccator flow into GASTEC (registered trademark) GV-100 and gas detector tube (No. .8H, 23M, 23L, manufactured by Gastec Corporation). Note that a small fan was housed in the desiccator together with the apparatus, and the air in the desiccator was convected by the small fan for 3 minutes prior to concentration measurement.

(実施例2,3)
亜塩素酸ナトリウム水溶液及びクエン酸水溶液の濃度を変更したことの他は、実施例1と同様にして装置を試作し、発生する二酸化塩素ガスの濃度を測定した。表1に亜塩素酸ナトリウム水溶液及びクエン酸水溶液の濃度を示す。
(Examples 2 and 3)
A device was made in the same manner as in Example 1 except that the concentrations of the sodium chlorite aqueous solution and the citric acid aqueous solution were changed, and the concentration of the generated chlorine dioxide gas was measured. Table 1 shows the concentrations of the sodium chlorite aqueous solution and the citric acid aqueous solution.

Figure 0005778991
Figure 0005778991

(比較例1)
濃度10質量%の亜塩素酸ナトリウム水溶液100mLにクエン酸含有ゲル化剤5.4gを添加することによって二酸化塩素ガスを発生させた。なお、クエン酸含有ゲル化剤は十分量のクエン酸を吸水ポリマーに吸収させることによって調製した。
(Comparative Example 1)
Chlorine dioxide gas was generated by adding 5.4 g of a citric acid-containing gelling agent to 100 mL of an aqueous sodium chlorite solution having a concentration of 10% by mass. The citric acid-containing gelling agent was prepared by allowing a water-absorbing polymer to absorb a sufficient amount of citric acid.

図6に実施例1〜3及び比較例1に係る装置から発生する二酸化塩素ガスの経時変化を示す。   FIG. 6 shows changes over time in chlorine dioxide gas generated from the apparatuses according to Examples 1 to 3 and Comparative Example 1.

実験の結果、実施例1〜3は、14日間にわたり安定した二酸化塩素濃度を維持したのに対して、比較例1では、5日を越えた時点で二酸化塩素濃度が大きく減少し、その後も減少しつづけた。このことから本発明に係る気体発生装置は、十分に長期にわたって安定的に気体を生じさせることが可能であることがわかった。   As a result of the experiment, Examples 1 to 3 maintained a stable chlorine dioxide concentration for 14 days, whereas in Comparative Example 1, the chlorine dioxide concentration decreased greatly after 5 days and decreased thereafter. Continued. From this, it was found that the gas generator according to the present invention can generate gas stably over a sufficiently long period of time.

1,11,21…第1の容器、2,12,22…第2の容器、1a,11a…第1の容器の開口、2a,12a…第2の容器の開口、3,13…吸液材、3a,3b…吸液部、3c…蒸散部、5,15…容器保持体、10,20…気体発生装置、13a,13b…領域(吸液部)、13c…領域(蒸散部)。 DESCRIPTION OF SYMBOLS 1, 11, 21 ... 1st container, 2, 12, 22 ... 2nd container, 1a, 11a ... Opening of 1st container, 2a, 12a ... Opening of 2nd container, 3, 13 ... Liquid absorption Material, 3a, 3b ... liquid absorption part, 3c ... transpiration part, 5, 15 ... container holder, 10, 20 ... gas generator, 13a, 13b ... area (liquid absorption part), 13c ... area (transpiration part).

Claims (4)

第1の液体を収容する第1の容器と、
第2の液体を収容する第2の容器と、
前記第1の液体と接触する第1の吸液部、前記第2の液体と接触する第2の吸液部、及び、前記第1の液体と前記第2の液体の化学反応による気体を生じさせる蒸散部を有する吸液材と、
を備える気体発生装置。
A first container containing a first liquid;
A second container containing a second liquid;
A first liquid-absorbing part that contacts the first liquid, a second liquid-absorbing part that contacts the second liquid, and a gas generated by a chemical reaction between the first liquid and the second liquid are generated. A liquid-absorbing material having a transpiration portion to be
A gas generator comprising:
前記気体は二酸化塩素又は二酸化炭素である、請求項1に記載の気体発生装置。   The gas generator according to claim 1, wherein the gas is chlorine dioxide or carbon dioxide. 前記第1の容器及び前記第2の容器を保持する容器保持体を更に備え、前記第1の容器及び前記第2の容器は前記吸液材が挿入される開口を上方にそれぞれ有し、前記蒸散部が前記第1の容器及び前記第2の容器の上方に配置されている、請求項1又は2に記載の気体発生装置。   A container holder for holding the first container and the second container; the first container and the second container each have an opening in which the liquid absorbing material is inserted; The gas generator according to claim 1 or 2, wherein a transpiration unit is disposed above the first container and the second container. 前記第1の容器及び前記第2の容器を保持する容器保持体を更に備え、前記第1の容器及び前記第2の容器は液体排出用の開口を下方にそれぞれ有し、前記蒸散部が前記第1の容器及び前記第2の容器の下方に配置されている、請求項1又は2に記載の気体発生装置。   A container holder for holding the first container and the second container; the first container and the second container each have an opening for discharging liquid; The gas generator according to claim 1, wherein the gas generator is disposed below the first container and the second container.
JP2011116998A 2011-05-25 2011-05-25 Gas generator Active JP5778991B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2011116998A JP5778991B2 (en) 2011-05-25 2011-05-25 Gas generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2011116998A JP5778991B2 (en) 2011-05-25 2011-05-25 Gas generator

Publications (2)

Publication Number Publication Date
JP2012246152A JP2012246152A (en) 2012-12-13
JP5778991B2 true JP5778991B2 (en) 2015-09-16

Family

ID=47466997

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2011116998A Active JP5778991B2 (en) 2011-05-25 2011-05-25 Gas generator

Country Status (1)

Country Link
JP (1) JP5778991B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101736825B1 (en) * 2015-10-28 2017-05-17 주식회사 이노푸스 An portable gasifier for even consistency of pure chlorine dioxiide

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104936687A (en) * 2012-12-25 2015-09-23 阿斯制药株式会社 Gas generation device and gas generation method

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2738728B2 (en) * 1988-12-16 1998-04-08 エステー化学株式会社 Method and apparatus for generating chlorine dioxide gas
US5091107A (en) * 1989-10-20 1992-02-25 The Drackett Company Chlorine dioxide generating device
US20050224750A1 (en) * 2002-04-29 2005-10-13 Seung-Hee Yang Simple apparatus for producing chlorine dioxide gas
JP4125103B2 (en) * 2002-12-10 2008-07-30 第一制電機株式会社 Chlorine dioxide gas generator
JP2007099568A (en) * 2005-10-05 2007-04-19 Takimoto Giken Kogyo Kk Apparatus for forming chlorine dioxide water
JP5140931B2 (en) * 2006-02-21 2013-02-13 カシオ計算機株式会社 Vaporizer, fuel cell equipped with vaporizer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101736825B1 (en) * 2015-10-28 2017-05-17 주식회사 이노푸스 An portable gasifier for even consistency of pure chlorine dioxiide

Also Published As

Publication number Publication date
JP2012246152A (en) 2012-12-13

Similar Documents

Publication Publication Date Title
US9333475B1 (en) Portable chlorine dioxide generator
JP6224007B2 (en) Gas generating apparatus and gas generating method
JP2016533777A (en) Hydrophilic IOL packaging system
JP2002510228A (en) Controlled release of substances
WO2015019984A1 (en) Beverage-containing pouch container and exterior sheet material therefor
US20160129147A1 (en) Spill-resistant air freshener canister
US20170304478A1 (en) Disinfectant wipe dispenser
JP5778991B2 (en) Gas generator
JP2014195776A (en) Urine encapsulation fluid
WO2019171639A1 (en) Cartridge, hydrogen gas inhaler, and hydrogen-gas-generating mixture
US20200391922A1 (en) Portable chlorine dioxide generator
WO2004049795A1 (en) Disposable, active substance-releasing electrical device
WO2015191811A1 (en) Cio2 on-demand disinfectant sponge or wipe and method of making
JP6208685B2 (en) Powder medicine injection device and powder medicine injection method
JP5730612B2 (en) Drug storage container and drug volatilization device
JP2013074819A (en) Toilet for animal
US20180154035A1 (en) Device for controlled release of fluid
KR20180121332A (en) Dehumidifying and deodorizing Container
JP2006167454A (en) Air treatment device for storing volatile chemical
JP5833902B2 (en) Heating transpiration device
JP6317957B2 (en) Disinfecting cotton container
JP4641857B2 (en) Package for medicine holder
WO2018161731A1 (en) Continuously extractable tissue paper
JP2001206429A (en) Dehumidifier container
US11279617B2 (en) Portable chlorine dioxide generator

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20140325

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20150121

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20150127

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20150707

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20150710

R150 Certificate of patent or registration of utility model

Ref document number: 5778991

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250