JP5806813B2 - Smoke device - Google Patents

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JP5806813B2
JP5806813B2 JP2010277297A JP2010277297A JP5806813B2 JP 5806813 B2 JP5806813 B2 JP 5806813B2 JP 2010277297 A JP2010277297 A JP 2010277297A JP 2010277297 A JP2010277297 A JP 2010277297A JP 5806813 B2 JP5806813 B2 JP 5806813B2
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smoke
agent
heating
container
side wall
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JP2011152127A5 (en
JP2011152127A (en
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小川 徹
徹 小川
耕平 松本
耕平 松本
片山 洋
洋 片山
昼間 徹夫
徹夫 昼間
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Lion Corp
Kyodo Printing Co Ltd
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Kyodo Printing Co Ltd
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Description

本発明は燻煙装置に関する。   The present invention relates to a smoke device.

ハエ、カ、ゴキブリ等の衛生害虫、細菌、カビ等の微生物等の有害生物の駆除等に、燻煙装置が汎用されている。燻煙装置は、燻煙剤又は燻蒸剤(以下、燻煙剤という)と、該燻煙剤を加熱する手段(加熱手段)とを有するものである。燻煙剤は、種々の燃焼剤又は発泡剤等を混合した発熱性基剤と、有効成分である薬剤とが主成分である。このような燻煙装置では、加熱手段により発熱性基剤を燃焼又は分解し、生じた燃焼熱又は分解熱で薬剤を気化し、空気中に放出、拡散する。あるいは、発熱性基剤の分解により発生するガス又は煙粒子の働きにより、気化した薬剤を短時間の内に空気中に放出、拡散する(以下、薬剤の空気中への放出、拡散を揮散という)。こうして揮散した薬剤により、有害生物の防除等を行うことのできる優れた製剤である。   Smoke devices are widely used to control sanitary pests such as flies, mosquitoes and cockroaches, and pests such as microorganisms such as bacteria and fungi. The smoke device includes a smoke agent or a fumigant (hereinafter referred to as smoke agent) and means for heating the smoke agent (heating means). Smoke agents are mainly composed of an exothermic base in which various combustion agents or foaming agents are mixed and a drug as an active ingredient. In such a smoke device, the exothermic base is combusted or decomposed by the heating means, the chemical is vaporized by the generated combustion heat or heat of decomposition, and is released and diffused into the air. Alternatively, the vaporized drug is released and diffused in the air within a short time by the action of gas or smoke particles generated by the decomposition of the pyrogenic base (hereinafter, the release and diffusion of the drug in the air is called volatilization. ). It is an excellent preparation capable of controlling pests and the like with the chemicals volatilized in this way.

一般的に、燻煙装置における燻煙剤の加熱は、燻煙剤の一部分をマッチで点火して燃焼させたり、酸化カルシウム等の加熱剤の水和反応熱により燻煙剤を加熱する手法が用いられる。例えば、加熱剤の水和反応熱を利用した燻煙装置としては、燻煙剤と加熱剤とを仕切る仕切部材を設け、この仕切部材を介して燻煙剤を加熱するものが提案されている(例えば、特許文献1〜3)。かかる燻煙装置では、燻煙剤の緩やかな燃焼の自己伝播により発熱性基剤が分解しガスを生じ、生じたガスの作用によって、薬剤が空間に揮散する。このように、燻煙装置は、燻煙剤中の発熱性基剤の燃焼等を利用するため、不燃性の容器が用いられている。不燃性の容器としては、アルミニウムやブリキ等の金属製缶が一般的である。昨今では、ブリキの代替として、錫を用いない鋼板であるTFS(ティンフリースティール)が用いられるようになっている。   In general, the heating of the smoke agent in the smoke device is a method in which a part of the smoke agent is ignited and burned with a match, or the smoke agent is heated by the hydration reaction heat of a heating agent such as calcium oxide. Used. For example, as a smoke device that uses the heat of hydration reaction of a heating agent, a device that provides a partition member that partitions the smoke agent and the heating agent and that heats the smoke agent via the partition member has been proposed. (For example, Patent Documents 1 to 3). In such a smoke device, the exothermic base decomposes and gas is generated by the self-propagation of the slow combustion of the smoke agent, and the chemical vapors into the space by the action of the generated gas. As described above, since the smoke device uses combustion of the exothermic base in the smoke agent, a non-combustible container is used. As the incombustible container, a metal can such as aluminum or tin is generally used. In recent years, TFS (Tin Free Steel), which is a steel sheet that does not use tin, has been used as an alternative to tinplate.

ところで、これらの金属製缶を用いた燻煙装置は、使用後に不燃物として廃棄するものである。このため、環境負荷が少ない廃棄処理の容易な燻煙装置が求められている。ここで、単に容器全体を紙製とした場合には、紙の熱伝導性が低いために、燻煙剤の加熱不足が生じ、薬剤の揮散が不十分になる。
このような課題に対して、安価かつ廃棄処理の簡便な、アルミラミネートの蓋を有する紙製のくん煙容器が提案されている(例えば、特許文献4)。また、例えば、紙層と合成樹脂層と金属層とからなる紙製容器を用いた自己発熱装置が提案されている(例えば、特許文献5)。
By the way, the smoke device using these metal cans is discarded as an incombustible material after use. For this reason, there is a need for a smoke device that has a low environmental impact and is easy to dispose of. Here, when the entire container is simply made of paper, the thermal conductivity of the paper is low, so that the smoke agent is insufficiently heated and the volatilization of the chemical becomes insufficient.
In order to deal with such problems, a paper smoke container having an aluminum laminate lid that is inexpensive and easy to dispose of has been proposed (for example, Patent Document 4). For example, a self-heating device using a paper container made of a paper layer, a synthetic resin layer, and a metal layer has been proposed (for example, Patent Document 5).

特開2002−338407号公報JP 2002-338407 A 特開2003−70404号公報JP 2003-70404 A 特開2007−326851号公報JP 2007-326851 A 特開平6−7065号公報JP-A-6-7065 特開2000−350547号公報JP 2000-350547 A

しかしながら、特許文献1〜3の燻煙装置は、薬剤の揮散効率の向上が図れるものの、金属素材を排除することは想定されておらず、環境負荷の低減の面で不十分であった。特許文献4、5の燻煙装置では、容器にアルミニウム箔等の金属素材が用いられている。加えて、特許文献5の自己発熱装置では、燻煙剤を内容器に充填し、該内容器を介して燻煙剤を加熱するため、前記内容器にも金属素材が用いられている。このため、環境負荷の低減の面で不十分であった。
そこで、本発明は、加熱剤で生じた熱を燻煙剤に損失なく素早く伝達しうることにより、金属素材を用いることなく薬剤を十分に揮散でき、環境負荷を低減できる燻煙装置を目的とする。
However, although the smoke device of patent documents 1-3 can aim at improvement in volatilization efficiency of a medicine, it is not assumed that a metal material is excluded, and is insufficient in terms of reduction of environmental load. In the smoke device of Patent Documents 4 and 5, a metal material such as an aluminum foil is used for the container. In addition, in the self-heating device of Patent Document 5, in order to fill the inner container with the smoke agent and to heat the smoke agent through the inner container, a metal material is also used for the inner container. For this reason, it was insufficient in terms of reduction of environmental load.
Therefore, the present invention aims at a smoke device capable of sufficiently transferring the heat generated by the heating agent to the smoke agent without loss, so that the chemical can be sufficiently volatilized without using a metal material, and the environmental load can be reduced. To do.

本発明の燻煙装置は略筒状の側壁部と、該側壁部の底面に設けられた底部とを有する容器を備え、前記容器は、可燃性の素材からなり、前記容器内の下方には、水和反応により発熱する加熱剤が充填されてなる加熱部が設けられ、前記容器内には、燻煙剤が充填されてなる燻煙剤部が設けられ、前記加熱部と前記燻煙剤部との間には、前記加熱剤の水和反応熱により溶融する素材からなる仕切部材が設けられていることを特徴とする。
前記側壁部は、紙製であることが好ましく、前記底部には、前記加熱部に水が流入する通水孔が形成されていることが好ましい。
The smoke device of the present invention includes a container having a substantially cylindrical side wall part and a bottom part provided on the bottom surface of the side wall part, and the container is made of a flammable material, A heating part filled with a heating agent that generates heat due to a hydration reaction is provided, and a smoke agent part filled with a smoke agent is provided in the container, and the heating part and the smoke agent A partition member made of a material that is melted by heat of hydration reaction of the heating agent is provided between the two parts.
The side wall portion is preferably made of paper, and a water passage hole through which water flows into the heating portion is preferably formed in the bottom portion.

本発明の燻煙装置によれば、加熱剤で生じた熱を燻煙剤に損失なく素早く伝達しうることにより、金属素材を用いることなく薬剤を十分に揮散でき、環境負荷を低減できる。   According to the smoke device of the present invention, the heat generated by the heating agent can be quickly transferred to the smoke agent without loss, so that the chemical can be sufficiently volatilized without using a metal material, and the environmental load can be reduced.

本発明の燻煙装置の一例を示す断面図である。It is sectional drawing which shows an example of the soot device of this invention. 本発明の燻煙装置の一例を示す断面図である。It is sectional drawing which shows an example of the soot device of this invention. 本発明の燻煙装置の一例を示す断面図である。It is sectional drawing which shows an example of the soot device of this invention.

本発明の燻煙装置の一実施形態について、図1を用いて説明する。図1は、本発明の燻煙装置8の断面図である。燻煙装置8は、容器10内に加熱部30と燻煙剤部20とを、仕切部材22を介して上下に隣接するように設けたものである。
容器10は、略円筒形の側壁部12と、側壁部12の天面側に設けられた蓋部14と、側壁部12の底面側に設けられた底部16とで概略構成されている。蓋部14には、気化した薬剤を流出させる通煙孔15が形成されている。
加熱部30は、容器10内の下方に充填された加熱剤からなるものである。仕切部材22は、容器10における蓋部14から底部16に向かうに従って、その径が小さくなる略円錐台の容器である。仕切部材22は、蓋部14側が開口部とされ、その開口部の周縁が側壁部12の内周面と接し、かつ底部16側が加熱部30の天面(加熱部天面)32と接して設けられたものである。仕切部材22には、燻煙剤が充填されて燻煙剤部20が設けられている。
An embodiment of the smoke device of the present invention will be described with reference to FIG. FIG. 1 is a cross-sectional view of the smoke device 8 of the present invention. In the smoke device 8, the heating unit 30 and the smoke agent unit 20 are provided in the container 10 so as to be adjacent to each other vertically through the partition member 22.
The container 10 is roughly configured by a substantially cylindrical side wall portion 12, a lid portion 14 provided on the top surface side of the side wall portion 12, and a bottom portion 16 provided on the bottom surface side of the side wall portion 12. The lid portion 14 is formed with a smoke hole 15 through which the vaporized medicine flows out.
The heating unit 30 is made of a heating agent filled in the lower part of the container 10. The partition member 22 is a substantially truncated cone container whose diameter decreases as it goes from the lid portion 14 to the bottom portion 16 of the container 10. The partition member 22 has an opening on the lid portion 14 side, the peripheral edge of the opening portion is in contact with the inner peripheral surface of the side wall portion 12, and the bottom portion 16 side is in contact with the top surface (heating portion top surface) 32 of the heating unit 30. It is provided. The partition member 22 is filled with a smoke agent and is provided with a smoke agent portion 20.

本実施形態の側壁部12は、可燃性の材質からなるものである。側壁部12の材質は、加熱剤の発熱温度に応じて決定することができる。例えば、加熱剤として酸化カルシウムを用いた場合、その水和反応により発熱温度は300〜400℃となる。従って、側壁部12には、このような温度においても溶融しない材質を選択する。このような側壁部12としては、例えば、紙類又は紙類の成形加工品である紙製の材料、パルプやコットン等の不織布、コルク等の木材製又はこれらにポリエチレン、ポリプロピレン、ポリエステル等の樹脂層を設けた積層物等が挙げられる。環境負荷の低減の観点からは、側壁部12は紙製の材料が好ましい。加えて、紙製の材料であれば、加工が容易である。   The side wall part 12 of this embodiment consists of a combustible material. The material of the side wall portion 12 can be determined according to the heat generation temperature of the heating agent. For example, when calcium oxide is used as the heating agent, the exothermic temperature becomes 300 to 400 ° C. due to the hydration reaction. Therefore, a material that does not melt even at such a temperature is selected for the side wall portion 12. As such a side wall part 12, for example, a paper material which is paper or a molded processed product of paper, a non-woven fabric such as pulp or cotton, a wood such as cork, or a resin such as polyethylene, polypropylene or polyester is used. Examples include a laminate provided with a layer. From the viewpoint of reducing environmental load, the side wall 12 is preferably made of paper. In addition, if it is a paper material, it will be easy to process.

紙類は、JIS P0001で定義される「紙」の他、JIS P0001で定義される「板紙」を含む概念である。また、紙製とは、紙類、JIS Z0104で定義される「段ボール」、JIS P0001で定義される不織布の内、紙の原料となるパルプを用いたものを含む概念である。   Paper is a concept including “paperboard” defined by JIS P0001 in addition to “paper” defined by JIS P0001. The term “made of paper” is a concept including paper, “corrugated cardboard” defined by JIS Z0104, and non-woven fabric defined by JIS P0001 using pulp as a raw material for paper.

側壁部12の材質としては、紙製の中でも、ライナー紙等の段ボール原紙、白板紙、色板紙等の紙器用板紙、防水原紙、紙管原紙等の雑板紙等の板紙、段ボールが好ましい。板紙、段ボールは、自立性を有するため成形が容易であると共に、高い断熱性を有するためである。   As the material of the side wall portion 12, among paper, cardboard base paper such as liner paper, paperboard paperboard such as white paperboard and color paperboard, paperboard such as miscellaneous paperboard such as waterproof base paper and paper tube base paper, and corrugated cardboard are preferable. This is because paperboard and corrugated cardboard are self-supporting and can be easily molded and have high heat insulation properties.

側壁部12として板紙を用いる場合、板紙の坪量は、例えば、200〜1000g/mが好ましく、400〜1000g/mがより好ましい。200g/m以上であれば、必要な自立性を有すると共に、断熱性が高まり、薬剤をより効率的に揮散できる。1000g/m以下であれば、成形が容易である。 When using paperboard as the side wall part 12, as for the basic weight of paperboard, 200-1000 g / m < 2 > is preferable and 400-1000 g / m < 2 > is more preferable, for example. If it is 200 g / m 2 or more, it has the necessary self-supporting property, and the heat insulating property is enhanced, so that the drug can be volatilized more efficiently. If it is 1000 g / m 2 or less, molding is easy.

側壁部12として段ボールを用いる場合、段ボールの坪量は、例えば、両面段ボール(中芯:Aフルート)であれば、200〜1000g/mが好ましく、500〜1000g/mがより好ましい。200g/m以上であれば、必要な自立性を有すると共に、断熱性が高まり、薬剤をより効率的に揮散できる。1000g/m以下であれば、成形が容易である。 When corrugated cardboard is used as the side wall part 12, the basis weight of the corrugated cardboard is preferably 200 to 1000 g / m 2 and more preferably 500 to 1000 g / m 2 if it is a double-faced cardboard (core: A flute). If it is 200 g / m 2 or more, it has the necessary self-supporting property, and the heat insulating property is enhanced, so that the drug can be volatilized more efficiently. If it is 1000 g / m 2 or less, molding is easy.

側壁部12にコルクを用いる場合、コルクの密度は、0.1〜0.5g/cmが好ましく、0.2〜0.4g/cmがより好ましい。0.1g/cm未満であると、強度が不十分となるおそれがあり、0.5g/cm超であると、断熱性が不十分となるおそれがある。 When using a cork for the side wall part 12, 0.1-0.5g / cm < 3 > is preferable and the density of a cork has more preferable 0.2-0.4g / cm < 3 >. If it is less than 0.1 g / cm 3 , the strength may be insufficient, and if it exceeds 0.5 g / cm 3 , the heat insulating property may be insufficient.

側壁部12の厚みは、側壁部12に求める強度、断熱性等を勘案して決定でき、例えば、1〜20mmとされる。   The thickness of the side wall portion 12 can be determined in consideration of the strength required for the side wall portion 12, the heat insulating property, and the like, and is set to 1 to 20 mm, for example.

側壁部12は、断熱性の高い材質を用いることが好ましい。例えば、側壁部は、断熱性の指標である熱伝導率が、好ましくは50%以下、より好ましくは30%以下である。50%以下であれば、薬剤を効率的に揮散できると共に、側壁部12の外周面の温度上昇を抑制できる。   The side wall 12 is preferably made of a highly heat-insulating material. For example, the side wall portion has a thermal conductivity that is an index of heat insulation, preferably 50% or less, more preferably 30% or less. If it is 50% or less, while being able to volatilize a chemical | medical agent efficiently, the temperature rise of the outer peripheral surface of the side wall part 12 can be suppressed.

蓋部14の材質は、側壁部12の材質と同様である。
通煙孔15の大きさは、気化した薬剤が流出できる大きさであればよい。また、通煙孔15の数量は特に限定されず、燻煙装置8の大きさや、燻煙剤の発煙量等を勘案して決定できる。
The material of the lid part 14 is the same as that of the side wall part 12.
The size of the smoke passage 15 may be a size that allows the vaporized medicine to flow out. Further, the number of the smoke passage holes 15 is not particularly limited, and can be determined in consideration of the size of the smoke device 8, the amount of smoke generated by the smoke agent, and the like.

底部16は、不織布からなるものである。不織布の材質は、加熱剤の発熱温度等を勘案して決定でき、例えば、ポリエチレン、ポリプロピレン、ポリエステル、パルプ、コットン等が挙げられる。不織布の種類は特に限定されず、例えば、スパンボンド、メルトブロー、サーマルボンド、ケミカルボンド、スパンレース、ニードルパンチ等の公知の製造方法により得られる不織布が挙げられる。   The bottom part 16 consists of a nonwoven fabric. The material of the nonwoven fabric can be determined in consideration of the heat generation temperature of the heating agent, and examples thereof include polyethylene, polypropylene, polyester, pulp, and cotton. The kind of nonwoven fabric is not specifically limited, For example, the nonwoven fabric obtained by well-known manufacturing methods, such as a spun bond, a melt blow, a thermal bond, a chemical bond, a spun lace, a needle punch, is mentioned.

仕切部材22の材質は、加熱剤の発熱により溶融するものであり、加熱剤の発熱温度に応じて選択することができ、例えば、ポリエチレン(融点:105〜115℃)、ポリプロピレン(融点:170℃)等のポリオレフィン、ポリエチレンテレフタレート(融点:260℃)等のポリエステル、ポリスチレン(融点:230℃)等のプラスチック製のフィルムや不織布等が挙げられる。例えば、加熱剤として酸化カルシウム(生石灰)を用いる場合、仕切部材22の材質は、融点:100〜300℃のものが好ましい。融点が100℃未満であると、高温下での保存により、溶融・変形するおそれがあり、融点が300℃超であると、酸化カルシウムの水和反応熱で仕切部材22が溶融しにくいためである。
加熱剤として酸化カルシウムを用いる場合、酸化カルシウムと水との反応により生じた水蒸気が、容器10内を上昇する。このため、仕切部材22としては、酸化カルシウムと水との反応初期に生じる水蒸気が、燻煙剤に接触するのを防ぐために、プラスチック製のフィルムを用いることが好ましい。
The material of the partition member 22 is melted by the heat generated by the heating agent, and can be selected according to the heat generation temperature of the heating agent. For example, polyethylene (melting point: 105 to 115 ° C.), polypropylene (melting point: 170 ° C.) ), Polyesters such as polyethylene terephthalate (melting point: 260 ° C.), plastic films such as polystyrene (melting point: 230 ° C.), and nonwoven fabrics. For example, when calcium oxide (quick lime) is used as the heating agent, the material of the partition member 22 is preferably one having a melting point of 100 to 300 ° C. If the melting point is less than 100 ° C., there is a risk of melting and deformation due to storage at high temperatures, and if the melting point exceeds 300 ° C., the partition member 22 is difficult to melt due to the heat of hydration reaction of calcium oxide. is there.
When calcium oxide is used as a heating agent, water vapor generated by the reaction between calcium oxide and water rises in the container 10. For this reason, it is preferable to use a plastic film as the partition member 22 in order to prevent water vapor generated in the initial reaction between calcium oxide and water from coming into contact with the smoke agent.

仕切部材22の厚さは、加熱剤の発熱温度や、仕切部材22の材質を勘案して決定でき、例えば、0.1〜0.5mmとすることが好ましい。上記範囲内とすることで、加熱剤の発熱により容易に溶融して燻煙剤が加熱剤と接触し、燻煙剤中の薬剤を効率的に気化できる。   The thickness of the partition member 22 can be determined in consideration of the heat generation temperature of the heating agent and the material of the partition member 22, and is preferably set to 0.1 to 0.5 mm, for example. By setting it within the above-mentioned range, it is easily melted by the heat generated by the heating agent, the smoke agent comes into contact with the heating agent, and the chemical in the smoke agent can be efficiently vaporized.

加熱部30に充填された加熱剤は、水との水和反応により任意の温度に発熱するものであり、例えば、酸化カルシウム、酸化マグネシウム、塩化アルミニウム、塩化カルシウム、酸化鉄等が挙げられ、中でも、取り扱いが容易であることから酸化カルシウムが好ましい。   The heating agent filled in the heating unit 30 generates heat at an arbitrary temperature by a hydration reaction with water, and examples thereof include calcium oxide, magnesium oxide, aluminum chloride, calcium chloride, and iron oxide. Calcium oxide is preferable because it is easy to handle.

加熱剤の充填量は、燻煙装置8の大きさや燻煙剤の量等を勘案して決定できる。例えば、加熱剤/燻煙剤の質量比は、2〜6.5とされる。   The filling amount of the heating agent can be determined in consideration of the size of the smoke device 8 and the amount of the smoke agent. For example, the mass ratio of the heating agent / smoke agent is 2 to 6.5.

燻煙剤部20に充填された燻煙剤は、薬剤を含有する。
薬剤は、例えば、殺虫剤、忌避剤、誘引剤、昆虫成長調節剤等の害虫駆除剤、抗菌剤、殺菌剤、防カビ剤等の微生物駆除剤、芳香剤、消臭剤等が挙げられる。害虫駆除剤としては、例えば、ペルメトリン、アレスリン、レスメトリン、サイフェノトリン、プラレスリン、フェノトリン、フェンバレレート、フェンプロパトリン、エトフェンプロックス等のピレスロイド系薬剤、フェニトロチオン、ジクロルボス(DDVP)、ダイアジノン、プロチオホス、バイテックス等の有機リン系薬剤、プロポクスル、メトキサジアゾン等のカーバメイト系薬剤等が挙げられる。微生物駆除剤としては、例えば、イソフタロニトリル、プロシミドン、バイレトン、モレスタン等の農薬用殺菌剤、サイアベンダゾール、3−ヨード−2−プロピニルブチルカーバメート(IPBC)、IF−1000等の環境衛生用殺菌剤等が挙げられる。
これらの薬剤は、1種単独で又は2種以上を適宜組み合わせて用いることができる。
The smoke agent filled in the smoke agent part 20 contains a medicine.
Examples of the drug include pest control agents such as insecticides, repellents, attractants, insect growth regulators, microbial control agents such as antibacterial agents, bactericides, and fungicides, fragrances, and deodorants. Pest control agents include, for example, permethrin, allethrin, resmethrin, cyphenothrin, prarestrin, phenothrin, fenvalerate, pyrethroids such as fenpropatoline, etofenprox, fenitrothion, dichlorvos (DDVP), diazinon, prothiophos, vitex And the like, and carbamate drugs such as propoxur and methoxadiazone. Examples of the microorganism-controlling agent include fungicides for agricultural chemicals such as isophthalonitrile, procymidone, bileton and morestan, sterilization for environmental health such as siabendazole, 3-iodo-2-propynylbutylcarbamate (IPBC) and IF-1000. Agents and the like.
These agents can be used singly or in appropriate combination of two or more.

燻煙剤中の薬剤の配合量は、薬剤の種類等を勘案して決定でき、例えば、1〜30質量%の範囲で決定することが好ましい。上記範囲内であれば、所望する薬剤効果が発揮されると共に、薬剤を効率的に揮散できる。   The blending amount of the drug in the smoke agent can be determined in consideration of the type of the drug, and is preferably determined in the range of 1 to 30% by mass, for example. If it is in the said range, while having the desired chemical | medical agent effect, a chemical | medical agent can be volatilized efficiently.

燻煙剤には、必要に応じ発熱性基剤を配合できる。発熱性基剤は、例えば、有機発泡剤や燃焼剤等、従来、燻煙剤に用いられる公知の発熱性基剤が挙げられる。中でも、発熱性基剤としては、有機発泡剤が好ましい。有機発泡剤には、加熱により熱分解して多量の熱を発生すると共に炭酸ガスや窒素ガス等(以下、総じてガスという)を発生するものが用いられる。有機発泡剤としては、例えば、アゾジカルボンアミド、ニトロセルロース、p,p’−オキシビス(ベンゼンスルホニルヒドラジド)、N,N’−ジニトロソペンタメチレンテトラミン、アゾビスイソブチロニトリル等が挙げられる。有機発泡剤の中でも、分解温度、ガス発生量等の観点から、アゾジカルボンアミドが好ましい。
これらの発熱性基剤は、1種単独で又は2種以上を適宜組み合わせて用いることができる。
An exothermic base can be blended with the smoke agent as necessary. Examples of the exothermic base include known exothermic bases conventionally used for smoke agents, such as organic foaming agents and combustion agents. Among these, an organic foaming agent is preferable as the exothermic base. As the organic foaming agent, those which are pyrolyzed by heating to generate a large amount of heat and generate carbon dioxide gas, nitrogen gas or the like (hereinafter generally referred to as gas) are used. Examples of the organic foaming agent include azodicarbonamide, nitrocellulose, p, p′-oxybis (benzenesulfonylhydrazide), N, N′-dinitrosopentamethylenetetramine, azobisisobutyronitrile, and the like. Among organic foaming agents, azodicarbonamide is preferable from the viewpoint of decomposition temperature, gas generation amount, and the like.
These exothermic bases can be used singly or in appropriate combination of two or more.

燻煙剤中の発熱性基剤の配合量は、薬剤の種類等を勘案して決定でき、例えば、50〜85質量%の範囲で決定することが好ましく、60〜75質量%の範囲で決定することがより好ましい。上記範囲内であれば、所望する薬剤効果が発揮されると共に、薬剤を効率的に揮散できる。   The blending amount of the exothermic base in the smoke agent can be determined in consideration of the type of the drug, and is preferably determined in the range of 50 to 85% by mass, for example, in the range of 60 to 75% by mass More preferably. If it is in the said range, while having the desired chemical | medical agent effect, a chemical | medical agent can be volatilized efficiently.

燻煙剤には、本発明の効果を疎外しない範囲で、発熱助剤、安定剤、結合剤、賦形剤、香料、色素等の添加剤を配合できる。これらのうち、特に、発熱助剤、安定剤、結合剤及び賦形剤のいずれか1種又は2種以上を含有することが好ましい。
発熱助剤としては、ステアリン酸亜鉛、ステアリン酸マグネシウム、酸化亜鉛、酸化マグネシウム、炭酸亜鉛、炭酸カルシウム、尿素等が挙げられる。
燻煙剤中、発熱助剤の含有量は、燻煙剤の総質量の0.1〜20質量%が好ましく、0.1〜15質量%がより好ましい。
In the smoke agent, additives such as exothermic aids, stabilizers, binders, excipients, fragrances, and pigments can be blended within the range that does not exclude the effects of the present invention. Among these, it is particularly preferable to contain one or more of exothermic assistants, stabilizers, binders and excipients.
Examples of the exothermic aid include zinc stearate, magnesium stearate, zinc oxide, magnesium oxide, zinc carbonate, calcium carbonate, urea and the like.
In the smoke agent, the content of the exothermic auxiliary is preferably 0.1 to 20% by mass, and more preferably 0.1 to 15% by mass of the total mass of the smoke agent.

安定化剤としては、ソルビタン脂肪酸エステル、ジブチルヒドロキシトルエン、ブチルヒドロキシアニソール、没食子酸プロピル、エポキシ化合物(エポキシ化大豆油、エポキシ化アマニ油等)等が挙げられる。
結合剤としては、メチルセルロース、エチルセルロース、カルボキシメチルセルロース、ヒドロキシプロピルメチルセルロース、ヒドロキシプロピルセルロース、デンプン、デキストリン、ヒドロキシプロピルスターチ、ゼラチン、ポリビニルアルコール、ポリビニルアセテート、ポリビニルピロリドン、ポリアクリル酸ナトリウム等が挙げられる。
賦形剤としては、クレー(含水ケイ酸アルミニウム)、タルク、珪藻土、カオリン、ベントナイト、ホワイトカーボン、炭酸カルシウム等が挙げられる。
Examples of the stabilizer include sorbitan fatty acid ester, dibutylhydroxytoluene, butylhydroxyanisole, propyl gallate, epoxy compounds (epoxidized soybean oil, epoxidized linseed oil, etc.) and the like.
Examples of the binder include methyl cellulose, ethyl cellulose, carboxymethyl cellulose, hydroxypropyl methyl cellulose, hydroxypropyl cellulose, starch, dextrin, hydroxypropyl starch, gelatin, polyvinyl alcohol, polyvinyl acetate, polyvinyl pyrrolidone, sodium polyacrylate, and the like.
Examples of the excipient include clay (hydrous aluminum silicate), talc, diatomaceous earth, kaolin, bentonite, white carbon, calcium carbonate and the like.

燻煙剤の充填量は、燻煙の対象とする空間の規模、燻煙剤中の薬剤の種類や配合量等を勘案して決定でき、例えば、6〜8畳(10〜13m)当たり10〜12.5gとされる。 The filling amount of the smoke agent can be determined in consideration of the size of the space to be smoked, the type and amount of the drug in the smoke agent, for example, 6 to 8 tatami mats (10 to 13 m 2 ) 10 to 12.5 g.

燻煙剤は、粉状、粒状、錠剤等の固形製剤として調製される。固形製剤は、目的とする剤形に応じて、公知の製造方法を用いて調製することができる。例えば、粒状の製剤とする場合は、押出し造粒法、圧縮造粒法、撹拌造粒法、転動造粒法、流動層造粒法等、公知の造粒物の製造方法により製造できる。
押出し造粒法による製造方法の具体例としては、燻煙剤の各成分を、ニーダー等により混合し、さらに適量の水を加えて混合し、得られた混合物を一定面積の開孔を有するダイスを用い、前押し出しあるいは横押し出し造粒機を用い造粒する。該造粒物は、さらにカッター等を用いて一定の大きさに切断し乾燥してもよい。
The smoke agent is prepared as a solid preparation such as powder, granules, and tablets. The solid preparation can be prepared using a known production method according to the intended dosage form. For example, in the case of a granular preparation, it can be produced by a known granulated production method such as extrusion granulation method, compression granulation method, stirring granulation method, tumbling granulation method, fluidized bed granulation method and the like.
As a specific example of the production method by the extrusion granulation method, each component of the smoke agent is mixed by a kneader and the like, and an appropriate amount of water is added and mixed, and the resulting mixture is a die having an opening of a certain area. And granulate using a pre-extrusion or horizontal extrusion granulator. The granulated product may be further cut into a certain size using a cutter or the like and dried.

次に、燻煙装置8を用いた燻煙方法について、発熱性基剤に有機発泡剤を用いた場合を例にして説明する。まず、水を入れた水収納容器を用意する。次いで、底部16が水に浸るように、燻煙装置8を前記水収納容器内に静置する。水収納容器内に燻煙装置8を静置すると、水が底部16を浸透して加熱部30に流入する。この段階では、仕切部材22の存在により、燻煙剤と加熱剤とが分離されている。このため、加熱部には加熱剤のみが存在するので、加熱剤は速やかに給水し、水和反応により発熱する。また、燻煙剤には、流入した水が接触していない。
水和反応で生じた水和反応熱により、燻煙剤が任意の温度に達すると、燻煙剤中の薬剤が気化すると共に、有機発泡剤が分解しガスを発生する。そして、気化した薬剤はガスと共に通煙孔15から流出し、空気中に拡散する。加えて、水和反応で生じた水和反応熱により、仕切部材22が溶融する。仕切部材22が溶融すると、仕切部材22に充填されている燻煙剤は、加熱部30上に撒かれ、加熱剤と直接接触する。このため、加熱剤の水和反応熱が燻煙剤に急速に伝播し、燻煙剤中の薬剤は短時間で効率的に揮散する。
Next, the smoke method using the smoke device 8 will be described by taking an example where an organic foaming agent is used as the exothermic base. First, prepare a water storage container containing water. Next, the smoke device 8 is placed in the water storage container so that the bottom 16 is immersed in water. When the smoke device 8 is left in the water storage container, water penetrates the bottom 16 and flows into the heating unit 30. At this stage, the smoke agent and the heating agent are separated by the presence of the partition member 22. For this reason, since only a heating agent exists in a heating part, a heating agent supplies water rapidly and it produces heat | fever by a hydration reaction. In addition, the inflowing water is not in contact with the smoke agent.
When the smoke agent reaches an arbitrary temperature due to the heat of hydration reaction generated by the hydration reaction, the agent in the smoke agent is vaporized and the organic foaming agent is decomposed to generate gas. And the vaporized chemical | medical agent flows out from the smoke vent 15 with gas, and is spread | diffused in the air. In addition, the partition member 22 is melted by the hydration reaction heat generated by the hydration reaction. When the partition member 22 melts, the smoke agent filled in the partition member 22 is spread on the heating unit 30 and directly contacts the heating agent. For this reason, the heat of hydration reaction of the heating agent rapidly propagates to the smoke agent, and the agent in the smoke agent is efficiently vaporized in a short time.

上述のとおり、本実施形態の燻煙装置は、金属素材を実質的に含まない可燃性の素材のみで構成されている。このため、燻煙装置は、使用後に可燃ごみとして廃棄することができ、環境負荷の低減が図れる。
加えて、燻煙剤部は、仕切部材を介して加熱部と隣接しているため、薬剤の気化又は有機発泡剤のガス発生に必要な水和反応熱が生じる前に燻煙剤が水に濡れることがなく、薬剤が速やかに気化する。また、薬剤の気化又は有機発泡剤のガス発生に必要な水和反応熱が生じた後は、加熱部で生じた水和反応熱が燻煙剤に直接伝えられ、短時間で薬剤を揮散できる。このように、燻煙開始直後から燻煙終了時に至るまで、燻煙剤を効率的に加熱でき、この結果、薬剤を効率的に揮散できる。加えて、薬剤の揮散を短時間で行うため、容器が加熱される時間も短くなり、可燃性の容器であっても、変形等を伴わず燻煙できる。
さらに、本発明の燻煙装置は、薬剤の揮散に際し、火炎を用いることがないため、容器自体が発火せず、安全に使用できる。
As described above, the smoke device of the present embodiment is composed of only a combustible material that does not substantially include a metal material. For this reason, the smoke device can be discarded as combustible waste after use, and the environmental load can be reduced.
In addition, since the smoke agent part is adjacent to the heating part via the partition member, the smoke agent is brought into water before the heat of hydration reaction necessary for the vaporization of the chemical or the gas generation of the organic foaming agent occurs. The drug vaporizes quickly without getting wet. In addition, after the heat of hydration reaction necessary for the vaporization of the drug or the gas generation of the organic foaming agent is generated, the heat of hydration reaction generated in the heating part is directly transmitted to the smoke agent, so that the drug can be volatilized in a short time. . Thus, the smoke agent can be efficiently heated from immediately after the start of smoke until the end of smoke, and as a result, the chemical can be efficiently vaporized. In addition, since the chemicals are volatilized in a short time, the time during which the container is heated is shortened, and even a flammable container can be smoked without deformation.
Furthermore, since the smoke device of the present invention does not use a flame when the chemical is volatilized, the container itself does not ignite and can be used safely.

本発明の燻煙装置は、上述の実施形態に限定されるものではない。
上述の実施形態では、側壁部の形状は円筒形である。しかしながら、側壁部の形状はこれに限定されず、例えば、横断面の形状が多角形の角筒形であってもよい。また、例えば、天面から底面に向かうに従って、その径が大きくなるような形状や、両端面から中央に向かうに従って、その径が大きくなるような形状であってもよい。
The smoke device of the present invention is not limited to the above-described embodiment.
In the above-described embodiment, the shape of the side wall portion is a cylindrical shape. However, the shape of the side wall portion is not limited to this, and for example, the shape of the cross section may be a polygonal rectangular tube. Further, for example, a shape in which the diameter increases from the top surface toward the bottom surface or a shape in which the diameter increases from the both end surfaces toward the center may be employed.

上述の実施形態では、容器の底部に不織布が用いられているが、底部はこれに限定されない。底部は、例えば、シート状の紙類、金属等に貫通孔を穿設したものであってもよいし、紙製、金属製のメッシュ等であってもよい。   In the above-mentioned embodiment, although the nonwoven fabric is used for the bottom part of a container, a bottom part is not limited to this. The bottom portion may be, for example, a sheet-like paper, a metal or the like with a through hole, or may be made of paper or a metal mesh.

上述の実施形態では、容器の下方に加熱剤が充填され、加熱部が設けられているが、本発明はこれに限定されない。例えば、加熱部には、加熱剤と共に、水を収容した容体が設置されていてもよい。このような加熱部では、燻煙時に該容体から水を放出することで、加熱剤との水和反応を発生することができる。このような加熱部を採用した場合には、底部16は、不織布等の透水性を有する素材や、通水孔を設けた部材でなくてもよい。   In the above-described embodiment, the heating agent is filled below the container and the heating unit is provided, but the present invention is not limited to this. For example, a container containing water may be installed in the heating unit together with the heating agent. In such a heating part, water can be released from the container during smoke so that a hydration reaction with the heating agent can occur. When such a heating unit is employed, the bottom portion 16 may not be a material having water permeability such as a nonwoven fabric or a member provided with water passage holes.

上述の実施形態では、仕切部材の形状は略円錐台とされているが、仕切部材の形状はこれに限定されない。例えば、図2の燻煙装置100のように、容器12内を鉛直方向に仕切るシート状の仕切部材122としてもよい。燻煙装置100においては、加熱部30上に仕切部材122を介して燻煙剤部120が載置された構成とされている。また、例えば、仕切部材は、円錐形、多角錐形、欠球形、円柱形、立方体形、袋状等としてもよい。   In the above-described embodiment, the shape of the partition member is substantially a truncated cone, but the shape of the partition member is not limited to this. For example, it is good also as the sheet-like partition member 122 which partitions off the inside of the container 12 to the perpendicular direction like the smoke apparatus 100 of FIG. In the smoke device 100, the smoke agent unit 120 is placed on the heating unit 30 via the partition member 122. For example, the partition member may have a conical shape, a polygonal pyramid shape, a spherical shape, a cylindrical shape, a cubic shape, a bag shape, or the like.

上述の実施形態では、燻煙剤部は、加熱部天面に載置された構造とされている。しかしながら、燻煙剤部の設置位置はこれに限定されず、例えば、燻煙剤部は、その一部又は全部が加熱部に埋まるように設けられていてもよい。   In the above-mentioned embodiment, the smoke agent part is set as the structure mounted in the heating part top surface. However, the installation position of the smoke agent part is not limited to this. For example, the smoke agent part may be provided so that part or all of the smoke agent part is embedded in the heating part.

上述の実施形態では、燻煙剤部が仕切部材を介して加熱部と隣接している、即ち、仕切部材が加熱部に接触しているが、本発明はこれに限定されず、例えば、図3の燻煙装置200のように、加熱部30と仕切部材22とが離間したものであってもよい。燻煙装置200において、加熱部天面32と仕切部材22の底面222とは、離間距離Dで離間している。
離間距離Dは、仕切部材22の材質、加熱剤の種類等を勘案して決定でき、例えば、20mm以下とされる。
ただし、より早期に、燻煙剤を加熱し始める観点からは、仕切部材が加熱部天面に接し、加熱剤部と燻煙剤部とが仕切部材を介して隣接していることが好ましい。
In the above-mentioned embodiment, the smoke agent part is adjacent to the heating part via the partition member, that is, the partition member is in contact with the heating part, but the present invention is not limited to this, for example, FIG. 3, the heating unit 30 and the partition member 22 may be separated from each other. In the smoke device 200, the heating unit top surface 32 and the bottom surface 222 of the partition member 22 are separated by a separation distance D.
The separation distance D can be determined in consideration of the material of the partition member 22, the type of heating agent, and the like, and is set to 20 mm or less, for example.
However, from the viewpoint of starting heating the smoke agent earlier, it is preferable that the partition member is in contact with the top surface of the heating unit and the heating agent portion and the smoke agent portion are adjacent to each other via the partition member.

上述の実施形態では、通煙孔が形成された蓋部が容器に設けられている。しかしながら、容器は、蓋部が設けられず、天面が開口した形態であってもよい。   In the above-mentioned embodiment, the cover part in which the smoke vent was formed is provided in the container. However, the container may be in a form in which the lid is not provided and the top surface is opened.

以下に、実施例を示して本発明をより詳細に説明するが、本発明はこれに限定されるものではない。   Hereinafter, the present invention will be described in more detail with reference to examples, but the present invention is not limited thereto.

(使用原料)
[燻煙剤]
<薬剤>
・ペルメトリン:エクスミン(商品名)、住友化学株式会社製
・メトキサジアゾン:エレミック(商品名)、住友化学株式会社製
(Raw materials used)
[Fumigant]
<Drug>
・ Permethrin: Exmine (trade name), manufactured by Sumitomo Chemical Co., Ltd. ・ Metoxadiazone: Elemic (trade name), manufactured by Sumitomo Chemical Co., Ltd.

<発熱性基剤>
・アゾジカルボンアミド(ADCA):ダイブローAC.2040(C)(商品名)、大日精化工業株式会社製
<Exothermic base>
Azodicarbonamide (ADCA): Die blow AC. 2040 (C) (trade name), manufactured by Dainichi Seika Kogyo Co., Ltd.

<発熱助剤>
・酸化亜鉛:日本薬局方 酸化亜鉛、真比重5.6g/cm(20℃)、堺化学工業株式会社製
<Exothermic aid>
-Zinc oxide: Japanese Pharmacopoeia Zinc oxide, true specific gravity 5.6 g / cm 3 (20 ° C), manufactured by Sakai Chemical Industry Co., Ltd.

<結合剤>
・ヒドロキシプロピルメチルセルロース(HPMC):メトローズ60SH−50(商品名)、信越化学工業株式会社製
<Binder>
・ Hydroxypropyl methylcellulose (HPMC): Metrows 60SH-50 (trade name), manufactured by Shin-Etsu Chemical Co., Ltd.

<賦形剤>
・クレー:NK−300(商品名)、昭和KDE株式会社製
<Excipient>
・ Clay: NK-300 (trade name), manufactured by Showa KDE Co., Ltd.

[加熱剤]
・酸化カルシウム:「特開平01−308825号」に記載の方法に従い、消石灰を二酸化炭素が存在しない条件下で、4時間、600℃に加熱して脱水させた粒径1〜5mmの粒状の酸化カルシウム。
[Heating agent]
Calcium oxide: Granular oxidation with a particle size of 1 to 5 mm obtained by dehydrating slaked lime by heating at 600 ° C. for 4 hours in the absence of carbon dioxide in accordance with the method described in “JP-A-01-308825” calcium.

<仕切部材>
・ポリエチレン製カップ(PEカップ):材質;ポリエチレン、厚み;0.3mm、寸法;天面φ61mm、底面φ42mm、高さ33mm
・ポリスチレン製カップ(PSカップ):材質;ポリスチレン、厚み;0.25mm、寸法;天面φ65mm、底面φ40mm、高さ35mm
・TFS製カップ(TFSカップ):材質;TFS(Tin Free Steel;缶飲料用で汎用の錫無し鋼板)、厚み;0.25mm、寸法;天面φ60mm、底面φ40mm、高さ35mm
・アルミニウム製カップ(Alカップ):材質;アルミニウム、厚み;0.01mm、寸法;天面φ60mm、底面φ40mm、高さ33mm
<Partition member>
・ Polyethylene cup (PE cup): material: polyethylene, thickness: 0.3 mm, dimensions: top surface φ61 mm, bottom surface φ42 mm, height 33 mm
Polystyrene cup (PS cup): material: polystyrene, thickness: 0.25 mm, dimensions: top surface φ65 mm, bottom surface φ40 mm, height 35 mm
-TFS cup (TFS cup): material: TFS (Tin Free Steel; general-purpose tin-free steel plate for can drinks), thickness: 0.25 mm, dimensions: top surface φ60 mm, bottom surface φ40 mm, height 35 mm
Aluminum cup (Al cup): material: aluminum, thickness: 0.01 mm, dimensions: top surface φ60 mm, bottom surface φ40 mm, height 33 mm

(実験例1)
厚み0.25mmのTFS(缶飲料用で汎用の錫無し鋼板)について、以下に示す方法により、熱伝導率を測定した。
ヒーター(CORNING PC−400D(タイテック株式会社製))の発熱面に熱電対A(CS−11E−010−1−TC1−AMP、アンリツ株式会社製)を接触させ、ヒーターを300℃に発熱させた。
TFSの平板(40mm×40mm)を試料とし、この試料の一方の面に熱電対B(ST−11E−015、アンリツ株式会社製)を貼り付けたものを用意した。試料の他方の面をヒーターの発熱面に接触させ、熱電対A及び熱電対Bで測定した温度をサーモロガー(AM−8000E、アンリツ株式会社製)で記録した。ヒーターの発熱面に試料を接触させてから1分後の測定結果を用い、下記(1)式にて熱伝導率を算出した。
(Experimental example 1)
The thermal conductivity of TFS (thin steel plate for can beverages and general-purpose tin-free steel) having a thickness of 0.25 mm was measured by the method described below.
A thermocouple A (CS-11E-010-1-TC1-AMP, manufactured by Anritsu Co., Ltd.) was brought into contact with the heating surface of the heater (CORNING PC-400D (manufactured by Taitec Corporation)), and the heater was heated to 300 ° C. .
A TFS flat plate (40 mm × 40 mm) was used as a sample, and a thermocouple B (ST-11E-015, manufactured by Anritsu Co., Ltd.) was attached to one surface of the sample. The other surface of the sample was brought into contact with the heating surface of the heater, and the temperature measured with thermocouple A and thermocouple B was recorded with a thermologger (AM-8000E, manufactured by Anritsu Corporation). The thermal conductivity was calculated by the following formula (1) using the measurement result one minute after the sample was brought into contact with the heating surface of the heater.

熱伝導率(%)=試料表面温度(℃)/ヒーター温度(℃)×100 ・・・(1)   Thermal conductivity (%) = sample surface temperature (° C.) / Heater temperature (° C.) × 100 (1)

(実験例2)
ライナー紙A(坪量400g/m、厚み1.3mmのライナー紙)について、実験例1と同様にして熱伝導率を求めた。
(Experimental example 2)
For liner paper A (liner paper having a basis weight of 400 g / m 2 and a thickness of 1.3 mm), the thermal conductivity was determined in the same manner as in Experimental Example 1.

(実験例3)
ライナー紙B(ライナー紙Aを2枚重ねたもの、坪量800g/m、厚み2.6mm)について、実験例1と同様にして熱伝導率を求めた。
(Experimental example 3)
For liner paper B (two sheets of liner paper A stacked, basis weight 800 g / m 2 , thickness 2.6 mm), thermal conductivity was determined in the same manner as in Experimental Example 1.

(実験例4)
ボール紙(坪量100g/m、厚み1.7mm)について、実験例1と同様にして熱伝導率を求めた。
(Experimental example 4)
The thermal conductivity of cardboard (basis weight 100 g / m 2 , thickness 1.7 mm) was determined in the same manner as in Experimental Example 1.

(実験例5)
段ボール(表面及び裏面;坪量180g/m、中芯;坪量160g/m,Aフルート、厚み5mm、坪量520g/mの両面段ボール)について、実験例1と同様にして熱伝導率を求めた。
(Experimental example 5)
For cardboard (front and back; basis weight 180 g / m 2 , core: basis weight 160 g / m 2 , A flute, thickness 5 mm, basis weight 520 g / m 2 double-sided cardboard), heat conduction in the same manner as in Experimental Example 1. The rate was determined.

(実験例6)
コルク(密度0.24g/cm、厚み2.0mm)について、実験例1と同様にして熱伝導率を求めた。
(Experimental example 6)
The thermal conductivity of cork (density 0.24 g / cm 3 , thickness 2.0 mm) was determined in the same manner as in Experimental Example 1.

Figure 0005806813
Figure 0005806813

表1に示すように、紙製又はコルクは、熱伝導率が50%以下であった。金属であるTFSは、熱伝導率が62.5%であった。   As shown in Table 1, the thermal conductivity of paper or cork was 50% or less. The metal TFS had a thermal conductivity of 62.5%.

(実施例1〜9、比較例2〜5)
[燻煙剤の調製]
表2〜3に示す燻煙剤混合物の組成に従い、水以外の成分をらいかい機(石川式攪拌らいかい機)に投入し混合した。混合後、水を加えさらに混合し、燻煙剤混合物を得た。得られた燻煙剤混合物を直径2mmの開孔を有するダイスの前押し出し造粒機(EXK−1、株式会社不二パウダル製)を用い造粒し造粒物を得た。得られた造粒物を長さ2〜5mmに切断し、70℃に設定した乾燥機(RT−120HL、アルプ株式会社製)により、109.5質量部から100質量部にまで乾燥させ、顆粒状の燻煙剤を得た。
(Examples 1-9, Comparative Examples 2-5)
[Preparation of smoke agent]
According to the composition of the smoke mixture shown in Tables 2 to 3, components other than water were introduced into a raking machine (Ishikawa-type stirring raking machine) and mixed. After mixing, water was added and further mixed to obtain a smoke mixture. The obtained smoke mixture was granulated using a die pre-extruder granulator (EXK-1, manufactured by Fuji Powder Co., Ltd.) having an opening having a diameter of 2 mm to obtain a granulated product. The obtained granulated product was cut to a length of 2 to 5 mm and dried from 109.5 parts by mass to 100 parts by mass with a dryer (RT-120HL, manufactured by Alp Co., Ltd.) set at 70 ° C. A smoke-like agent was obtained.

[燻煙装置の作製]
表2〜3の仕様に従い、図1の燻煙装置8と同様の燻煙装置を作製した。蓋部は、表2〜3に記載の材質を材料とし、該材料の中央にφ9mmの通煙孔(中央通煙孔)を1個設け、さらに、中央通煙孔の周縁回りに、φ6mmの通煙孔を等間隔で4個設けたものとした。また、底部は、表2〜3の材質を材料とし、該材料の中央にφ9mmの通水孔(中央通水孔)を1個設け、中央通水孔の周縁回りに、φ6mmの通水孔を等間隔で4個設けたものとした。側壁部は、直径65mm、高さ50mmの円筒とした。側壁部に底部を装着し有底筒状の容体とし、該容体に加熱剤40gを充填し加熱部とした。
仕切部材の底面が加熱部天面と接触するように、仕切部材を側壁部に固定した。仕切部材に「[燻煙剤の調製]」で得られた燻煙剤10gを充填した。燻煙剤を充填後、容体に蓋部を装着し、燻煙装置を作製した。作製した燻煙装置にて燻煙を行い、揮散率を求めた。求めた揮散率を表2〜3に示す。
[Production of smoke device]
According to the specifications of Tables 2 and 3, a smoke device similar to the smoke device 8 of FIG. 1 was produced. The lid is made of the materials listed in Tables 2-3, and has one φ9 mm smoke vent (central smoke vent) in the center of the material, and further, a φ6 mm smoke vent around the periphery of the central smoke vent. Four holes were provided at equal intervals. In addition, the bottom portion is made of the materials shown in Tables 2 and 3, and one φ9 mm water passage hole (central water passage hole) is provided at the center of the material, and a φ6 mm water passage hole is provided around the periphery of the central water passage hole. Four pieces were provided at intervals. The side wall portion was a cylinder having a diameter of 65 mm and a height of 50 mm. A bottom portion was attached to the side wall portion to form a bottomed cylindrical container, and the container was filled with 40 g of a heating agent to form a heating section.
The partition member was fixed to the side wall portion so that the bottom surface of the partition member was in contact with the top surface of the heating unit. The partition member was filled with 10 g of the smoke agent obtained in “[Preparation of smoke agent]”. After filling with the smoke agent, a lid was attached to the container to produce a smoke device. Smoke was conducted with the produced smoke device to determine the volatilization rate. The calculated volatilization rates are shown in Tables 2-3.

(実施例10)
仕切部材の底面と加熱部天面とが離間(離間距離D=10mm)するように仕切部材を設け、図3に示す燻煙装置200と同様の燻煙装置とした以外は、実施例1と同様にして、燻煙装置を作製した。作製した燻煙装置にて燻煙を行い、揮散率を求めた。求めた揮散率を表3に示す。
(Example 10)
Example 1 except that the partition member is provided so that the bottom surface of the partition member and the top surface of the heating unit are separated (separation distance D = 10 mm), and the smoke device is similar to the smoke device 200 shown in FIG. Similarly, a smoke device was produced. Smoke was conducted with the produced smoke device to determine the volatilization rate. The calculated volatilization rate is shown in Table 3.

(比較例1)
側壁部及び蓋部の材質をTFS、底部として不織布を、通水孔を設けずに用いた以外は、実施例1と同様にして、燻煙装置を作製した。作製した燻煙装置にて燻煙を行い、揮散率を求めた。求めた揮散率を表3に示す。
(Comparative Example 1)
A smoke smoking apparatus was produced in the same manner as in Example 1 except that TFS was used as the material for the side wall and the lid, and non-woven fabric was used as the bottom without providing a water passage hole. Smoke was conducted with the produced smoke device to determine the volatilization rate. The calculated volatilization rate is shown in Table 3.

(比較例6)
[燻煙剤の調製]
表3に示す組成に従い、実施例1と同様にして燻煙剤を得た。
(Comparative Example 6)
[Preparation of smoke agent]
According to the composition shown in Table 3, a smoke agent was obtained in the same manner as in Example 1.

[燻煙装置の作製]
仕切部材を設けず、燻煙剤と加熱剤との混合物を容器に充填した以外は、実施例1と同様にして燻煙装置を作製した。作製した燻煙装置にて燻煙を行い、揮散率を求めた。求めた揮散率を表3に示す。
[Production of smoke device]
A smoke device was produced in the same manner as in Example 1 except that the partition member was not provided and the container was filled with a mixture of the smoke agent and the heating agent. Smoke was conducted with the produced smoke device to determine the volatilization rate. The calculated volatilization rate is shown in Table 3.

(評価方法)
[揮散率]
プラスティックカップ(水ではじめるバルサン(商品名、ライオン株式会社製)25g用)に水23mLを入れ、該プラスティックカップを内容積6.38m(6380L)の試験室の中央に設置した。該プラスティックカップに、各例の燻煙装置を静置し、燻煙を開始した。燻煙開始5分後に、試験室内の空気をファンで攪拌した。攪拌後、真空ポンプを用いて試験室内の空気20Lを回収用カラムに通流し、試験室内に揮散した薬剤を吸着させた。該回収用カラムには、クロマト用シリカゲル(Wakogel C−100、和光純薬工業株式会社製)を用いた。
次いで、薬剤を吸着させた後、アセトンを回収用カラムに通流し、通流したアセトンを回収した。こうして、クロマト用シリカゲルに吸着した薬剤を溶出させた。回収したアセトンを試料として、ガスクロマトグラフ法によりアセトン中の薬剤量(A)を定量した。一方、燻煙剤中の薬剤量(B)をガスクロマトグラフ法により定量した。これらの定量結果から、下記(2)式により揮散率を算出した。
(Evaluation method)
[Volatilization rate]
23 mL of water was placed in a plastic cup (for 25 g of Balsan (trade name, manufactured by Lion Corporation) starting with water), and the plastic cup was installed in the center of a test chamber having an internal volume of 6.38 m 3 (6380 L). The smoke device of each example was allowed to stand in the plastic cup, and smoke was started. Five minutes after the start of soot, the air in the test chamber was stirred with a fan. After stirring, 20 L of air in the test chamber was passed through the recovery column using a vacuum pump, and the volatilized chemical was adsorbed in the test chamber. As the recovery column, chromatographic silica gel (Wakogel C-100, manufactured by Wako Pure Chemical Industries, Ltd.) was used.
Next, after the drug was adsorbed, acetone was passed through the collection column, and the passed acetone was collected. Thus, the drug adsorbed on the silica gel for chromatography was eluted. Using the collected acetone as a sample, the amount of drug (A) in acetone was quantified by gas chromatography. On the other hand, the amount of chemical (B) in the smoke was determined by gas chromatography. From these quantitative results, the volatilization rate was calculated by the following formula (2).

揮散率(質量%)=(A/20L)×(1/B)×6380L×100%・・・(2)   Volatilization rate (mass%) = (A / 20L) × (1 / B) × 6380L × 100% (2)

[変形の有無]
各例の燻煙装置について、燻煙後の容器の状態を目視で確認し、下記評価基準により評価した。
変形「無」:側壁部、蓋部及び底部の変形がなく、側壁部と蓋部との接合部又は側壁部と底部との接合部のずれや緩みがない。
変形「有」:側壁部、蓋部又は底部のいずれかに変形があるか、側壁部と蓋部との接合部又は側壁部と底部との接合部のずれ又は緩みがある。
[Presence of deformation]
About the soot apparatus of each example, the state of the container after soot was confirmed visually, and the following evaluation criteria evaluated.
Deformation “No”: There is no deformation of the side wall, the lid and the bottom, and there is no displacement or loosening of the joint between the side wall and the lid or the joint between the side wall and the bottom.
Deformation “present”: There is deformation in any of the side wall part, the lid part or the bottom part, or there is a shift or looseness of the joint part between the side wall part and the lid part or the joint part between the side wall part and the bottom part.

Figure 0005806813
Figure 0005806813

Figure 0005806813
Figure 0005806813

実施例1〜10及び比較例1〜6は、燻煙時に容器の発火は認められなかった。実施例1〜10、比較例1、4〜6の容器は、燻煙終了時においても変形は認められなかった。一方、比較例2〜3の容器は、燻煙終了時において自立性を有していたものの、部分的な変形が認められた。比較例2〜3は、仕切部材を金属製としたため、仕切部材による放射熱の影響で変形が生じたと推測される。   In Examples 1 to 10 and Comparative Examples 1 to 6, the ignition of the container was not observed during soot. In the containers of Examples 1 to 10 and Comparative Examples 1 and 4 to 6, no deformation was observed even at the end of smoking. On the other hand, although the containers of Comparative Examples 2 to 3 were self-supporting at the end of smoking, partial deformation was observed. In Comparative Examples 2 to 3, since the partition member is made of metal, it is presumed that deformation occurred due to the influence of radiant heat by the partition member.

表2〜3に示すように、本発明を適用した実施例1〜10は、いずれも揮散率が60質量%以上であった。これに対し、表3に示すように、仕切部材を金属製とした比較例2〜5は、揮散率が53質量%以下であった。中でも、予め燻煙剤と加熱剤とを混合し充填した比較例6は、ペルメトリンの揮散率が19質量%、メトキサジアゾンの揮散率が32質量%と極めて低いものであった。
これらの結果から、本発明の燻煙装置は、加熱剤の水和反応熱により溶融する仕切部材を設けることで、側壁部を紙製としても、薬剤を効率的に揮散できることが判った。
As shown in Tables 2 and 3, the volatilization rate of each of Examples 1 to 10 to which the present invention was applied was 60% by mass or more. On the other hand, as shown in Table 3, in Comparative Examples 2 to 5 in which the partition member was made of metal, the volatilization rate was 53% by mass or less. Among them, in Comparative Example 6 in which the smoke agent and the heating agent were mixed and filled in advance, the volatilization rate of permethrin was 19% by mass, and the volatilization rate of methoxadiazone was 32% by mass.
From these results, it was found that the smoke smoking apparatus of the present invention can efficiently volatilize the drug even if the side wall is made of paper by providing a partition member that melts by the hydration reaction heat of the heating agent.

実施例1、7〜9は、燻煙剤中の有機発泡剤の組成が45〜70質量%であり、揮散率は65質量%以上であった。対して、比較例1〜6は燻煙剤中の有機発泡剤の組成が65質量%であり、揮散率はいずれも53質量%以下であった。
これらの結果から、本発明の燻煙装置は、仕切部材を金属製とする燻煙装置に比べ、燻煙剤中の有機発泡性が少なくても、薬剤を効率的に揮散できることが判った。
In Examples 1 and 7 to 9, the composition of the organic foaming agent in the smoke agent was 45 to 70% by mass, and the volatilization rate was 65% by mass or more. On the other hand, in Comparative Examples 1 to 6, the composition of the organic foaming agent in the smoke agent was 65% by mass, and the volatilization rate was 53% by mass or less.
From these results, it was found that the smoke device of the present invention can efficiently volatilize the chemical even if the organic foaming property in the smoke agent is small as compared with the smoke device in which the partition member is made of metal.

8、100、200 燻煙装置
10 容器
12 側壁部
15 通煙孔
16 底部
20、120 燻煙剤部
22、122 仕切部材
30 加熱部
8, 100, 200 Smoke device 10 Container 12 Side wall part 15 Smoke hole 16 Bottom part 20, 120 Smoke agent part 22, 122 Partition member 30 Heating part

Claims (3)

略筒状の側壁部と、該側壁部の底面に設けられた底部とを有する容器を備え、
前記容器は、可燃性の素材からなり、
前記側壁部は、下記測定方法で求められる熱伝導率が50%以下であり、
前記容器内の下方には、水和反応により発熱する加熱剤が充填されてなる加熱部が設けられ、
前記容器内には、燻煙剤が充填されてなる燻煙剤部が設けられ、
前記加熱部と前記燻煙剤部との間には、前記加熱剤の水和反応熱により溶融する仕切部材が設けられていることを特徴とする燻煙装置。
<測定方法>
ヒーターの発熱面に熱電対Aを接触させ、ヒーターを300℃に発熱させる。試料の一方の面に熱電対Bを貼り付けたものを用意する。試料の他方の面をヒーターの発熱面に接触させ、熱電対A及び熱電対Bで測定した温度を記録する。ヒーターの発熱面に試料を接触させてから1分後の測定結果を用い、下記(1)式にて熱伝導率を算出する。
熱伝導率(%)=試料表面温度(℃)/ヒーター温度(℃)×100・・・(1)
A container having a substantially cylindrical side wall and a bottom provided on the bottom surface of the side wall;
The container is made of a flammable material,
The side wall has a thermal conductivity of 50% or less determined by the following measurement method,
Below the inside of the container is provided a heating unit filled with a heating agent that generates heat by a hydration reaction,
In the container, a smoke agent part filled with a smoke agent is provided,
Between the heating part and the smoke agent part, a partition member that melts due to heat of hydration reaction of the heating agent is provided.
<Measurement method>
A thermocouple A is brought into contact with the heating surface of the heater, and the heater is heated to 300 ° C. Prepare a sample with thermocouple B attached to one side of the sample. The other surface of the sample is brought into contact with the heating surface of the heater, and the temperature measured with thermocouple A and thermocouple B is recorded. Using the measurement result one minute after the sample is brought into contact with the heating surface of the heater, the thermal conductivity is calculated by the following equation (1).
Thermal conductivity (%) = sample surface temperature (° C.) / Heater temperature (° C.) × 100 (1)
前記仕切部は、前記加熱部の上方に設けられ、前記容器の底部に向かうに従い径が小さくなり、内部に前記燻煙剤が充填されて前記燻煙剤部が設けられていることを特徴とする請求項1に記載の燻煙装置。 The partition part is provided above the heating part, and the diameter decreases toward the bottom of the container, and the smoke agent part is provided by being filled with the smoke agent. The smoke device according to claim 1. 前記底部には、前記加熱部に水が流入する通水孔が形成されていることを特徴とする、請求項1又は2に記載の燻煙装置。   The smoke device according to claim 1 or 2, wherein a water passage hole through which water flows into the heating unit is formed in the bottom portion.
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