WO1998035552A1 - Heat-generating agent for heating fumigant - Google Patents

Heat-generating agent for heating fumigant Download PDF

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Publication number
WO1998035552A1
WO1998035552A1 PCT/JP1998/000637 JP9800637W WO9835552A1 WO 1998035552 A1 WO1998035552 A1 WO 1998035552A1 JP 9800637 W JP9800637 W JP 9800637W WO 9835552 A1 WO9835552 A1 WO 9835552A1
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Prior art keywords
agent
calcium oxide
heating
water
heat
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PCT/JP1998/000637
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French (fr)
Japanese (ja)
Inventor
Kenji Takita
Original Assignee
Chugai Seiyaku Kabushiki Kaisha
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Priority to AU58814/98A priority Critical patent/AU5881498A/en
Publication of WO1998035552A1 publication Critical patent/WO1998035552A1/en

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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K5/00Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
    • C09K5/16Materials undergoing chemical reactions when used
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N25/00Biocides, pest repellants or attractants, or plant growth regulators, characterised by their forms, or by their non-active ingredients or by their methods of application, e.g. seed treatment or sequential application; Substances for reducing the noxious effect of the active ingredients to organisms other than pests
    • A01N25/20Combustible or heat-generating compositions

Definitions

  • the present invention relates to an exothermic agent for heating a smoke agent containing highly active calcium oxide and a method for heating the smoke agent using heat generated by a hydration reaction of calcium oxide with high activity.
  • Smoke-killers are agents that smoke pest control substances by heating.
  • a smoker containing a self-combustible substance such as nitrocellulose is reacted with a metal oxide and silicon (a so-called thermite reaction).
  • a direct heating method is known, in which the smoke is itself self-burned by directly heating (igniting) at once using the heat generated by the fumes.
  • the heating method by the thermit reaction is disclosed in Japanese Utility Model Application Laid-Open No. 62-144627 and Japanese Patent Laid-Open No. 1-288218.
  • the heating method by thermite reaction is based on the combustion reaction, so the temperature rises more than necessary at the time of heating, so that the active ingredient in the smoke agent may cause thermal decomposition.
  • the active ingredient in the smoke agent may cause thermal decomposition.
  • Japanese Utility Model Publication No. 5-69922 discloses that quicklime is tableted and molded into a ring or a cylinder and used as a heating element for heating cans.
  • the heating element is merely intended to fill the container, prevent the heating agent from flying off, and uniformly heat the can. The amount of heat required to initiate smoke in a short time after adding water is insufficient.
  • the present invention provides a heat generating apparatus for heating a smoking agent containing calcium oxide, which causes less thermal decomposition of the active ingredient, efficiently heats the smoking agent, and starts smoking immediately. It is intended to provide an agent.
  • the present inventors have conducted intensive studies on a method of heating a smoke agent using high heat generated by a hydration reaction of calcium oxide, and as a result, the heat generation rate when 20 g of calcium oxide was reacted with 6 ml of water. Calcium oxide at a temperature of 5 ° C / sec or more is subjected to a hydration reaction. Can be heated to the desired temperature.
  • the size is smaller than that of a conventional smoker container that uses unformed calcium oxide as a heating agent. It has become possible to make lightweight containers.
  • the present invention provides a heating agent for heating a smoking agent containing calcium oxide having a heat generation rate of 5 ° CZ seconds or more when 20 g of calcium oxide is reacted with 6 ml of water.
  • Book The exothermic agent of the invention is shaped so that the maximum temperature of the surface of the exothermic agent is equal to or higher than the fuming temperature of the smoking agent to be heated by heat generated when calcium oxide is reacted with water. Good.
  • the tableting pressure at that time is preferably from 200 to 400 kg / cm 2 .
  • it is tablet-formed into a shape of a perforated molded body. Examples of the shape of the perforated molded body include a cylindrical shape, a ring shape, and a cup shape.
  • the present invention also provides a method for heating a smoking agent by heat generated when calcium oxide having a heat generation rate of 5 ° CZ seconds or more (when 20 g of calcium oxide is reacted with 6 ml of water) is reacted with water. And a method for heating a smoking agent. Less than 100% by weight of calcium oxide, based on the total weight of the smoke agent to be heated, may be reacted with water. Preferably, calcium oxide is reacted with water in the presence of an inorganic acid and Z or an organic acid.
  • Drugs that can be used as fumigation agents include insecticides, various germicides I] ⁇ and their mixtures according to the purpose.
  • insecticides include, for example, pyrethroids such as permethrin, seculin, resmethrin, cyphenothrin, pralethrin, phenothrin, humvalerate, fenprono, ° trin, etofenprox, etc.
  • Organic drugs such as organic compounds, phennitrothion, dichlorvos (DDVP), diazinon, protifos, and vitex, and carbamates such as propoxur and methoxadiazon.
  • fungicides examples include fungicides for agricultural chemicals such as isophthalonitrile, procymidone, biletone, and molestan, thiabendazole, 3-odo-2—propynylbutyl carbamate (IPBC), IF-100, etc.
  • IPBC 3-odo-2—propynylbutyl carbamate
  • IF-100 IF-100
  • Environmental sanitizing germicides can be used.
  • the content of the above drug is preferably 2% by weight or more and 20% by weight or less based on the total weight of the smoking agent.
  • the heating method of the present invention can be used for both smokers heated by the direct heating method and smokers heated by the indirect heating method.
  • Such fumigation agents include the above-mentioned chemicals, heat generation agents for fumigation agents, heat-generating aids such as melamine and zinc oxide, and inorganic minerals such as clay, kaolin, talc, and diatomaceous earth. Addition is also possible.
  • binders and fragrances such as carboquine methylcellulose, hydroxyquinepropyl methylcellulose, polyvinyl alcohol, starch, potency enhancers such as piperonyl butoxide, S-421, and oxidation of BHT, tocoprole, etc.
  • An additive such as an inhibitor may be contained.
  • the present invention provides a smoker heating device in which the above-mentioned exothermic agent is housed in a container, wherein the container is capable of efficiently transmitting heat generated by a hydration reaction or the like to the smoker in contact with the container. It should be something you can do. For example, preferably, 5 W / m '° C or higher, more favorable Mashiku as container according good c container having a 1 0 WZm ⁇ ° C or more heat conductivity (the case of 2 5 ° C), Examples include those made of a material selected from aluminum, tin, copper, iron, and the like. Further, the container further when it c being sealed Further, the present invention provides a fumigant kit containing the above-described heating agent and smoking agents. The smoker may be either a smoker heated by a direct heating method or a smoker heated by an indirect heating method as described above.
  • the “heat generation rate” indicates an average temperature increase per second from the start time of heat generation by the hydration reaction of calcium oxide and water to the time to reach the maximum temperature.
  • the heat generation rate is 25 ° C or room temperature.
  • Powder or granules of calcium oxide are placed in a glass tube at 2 Og, and hydrated with 6 ml of water. Can be determined by measuring the maximum internal temperature and calculating the average temperature rise per second from the start of the hydration reaction to the maximum temperature.
  • the heat generation rate of calcium oxide which has been conventionally used for heating a smoking agent, is about 3 ns or less when 20 g of oxidizing power is reacted with 6 ml of water.
  • the heat generation rate of calcium oxide used in the present invention is at least 5 ° CZ seconds, preferably at least 6 ° CZ seconds when 20 g of calcium oxide is reacted with 6 ml of water.
  • the heat generation rate when reacting 20 g of calcium oxide with 6 ml of water used in the present invention is 5 ° C / sec.
  • the above calcium oxide is hereinafter referred to as “highly active calcium oxide”.
  • the “perforated molded body” in the present invention is a columnar, cubic, It refers to a molded article such as a rectangular parallelepiped, polygonal column, polygon, or sphere, and the hole may or may not penetrate the molded article. When the hole does not penetrate, it is desirable that the depth of the hole is not less than 1/3 of the thickness of the molded body.
  • Examples of such a perforated formed body include a formed body having a cylindrical shape, a ring shape, a cup shape, and the like.
  • Highly active calcium oxide is, for example, a method of dehydrating slaked lime by heating it to 550 to 770 ° C for about 10 minutes to 6 hours under conditions substantially free of carbon dioxide. (See Japanese Patent Application Publication No. 1-3088885).
  • the powdered granules of highly active calcium oxide produced by the above method may be used as they are, but preferably, they are compressed into tablets by a conventional method, and Into a ring, ring, cup, etc.
  • the tableting pressure at this time is preferably from 200 to 400 kg / cm 2 . If the tableting pressure is less than 200 kg / cm 2, it is difficult to obtain a good molded product, and if it exceeds 400 kg / cm 2 , cracks may occur in the molded product.
  • a lubricant such as magnesium stearate, calcium stearate, talc, or sodium lauryl sulfate further improves tableting moldability. can do.
  • the dimensions of the tablet diameter ( ⁇ ) and hole diameter ( ⁇ ) are not particularly specified. It may be determined according to the desired calorific value and the size of the storage container.
  • the ratio ( ⁇ 2Z01) of the tableting diameter ( ⁇ 1) to the hole diameter ( ⁇ 2) is 0.1 to 0.8, preferably 0.2. ⁇ 0.5.
  • the weight of each molded article varies depending on the desired calorific value, but is generally 1 to 24 g, preferably 2 to 15 g.
  • the heat generating agent for heating a smoking agent of the present invention can be used alone, or can be used by stacking a plurality of them.
  • the heating agent for heating the smoker of the present invention requires much more weight than the conventional smoker for heating and smoking the calcium oxide for heating the smoker.
  • the smoker can be heated and smoked with a smaller weight of calcium oxide than the smoker.
  • the exothermic agent for smokers of the present invention becomes apparently more specific by tableting, and it is possible to design a container form with a smaller heating space than before, and it is possible to make it smaller than before. ⁇ It is possible to design a smoker container that is lighter.
  • the exothermic agent for heating the smoking agent of the present invention is sealed in a highly heat-conductive container made of aluminum, tin, copper, iron, or the like, so that the heating of the smoking agent, which has been reduced in size and weight, can be performed. Equipment can be made.
  • the method of heating a smoke agent with calcium oxide has been to heat the smoke agent from the outside of the container containing the smoke agent.
  • a smoker container that heats the smoker by installing a heating device inside the container that holds the smoker, making the smoker smaller and lighter than before. It is feasible to design a smoke agent vessel.
  • the above-described heating device can be used as an ignition device for directly heating a smoking agent containing a self-combustible substance, instead of an ignition device using reaction heat of a thermite reaction.
  • the heating device it is possible to suppress the thermal decomposition of the active ingredient at the time of ignition of the smoking agent, as compared with the ignition by the reaction heat of the thermite reaction.
  • the heating of the smoking agent is good even if the hydration reaction is performed with only water, but in the presence of an inorganic acid and / or an organic acid.
  • the smoker can be heated more efficiently, and the time until smoke starts can be adjusted.
  • the addition of the acid further increases the maximum surface temperature.
  • examples of the inorganic acid include boric acid, nitric acid, hydrochloric acid, perchloric acid and the like.
  • examples of the organic acid include succinic acid, oxalic acid, lingic acid, ascorbic acid, and citric acid.
  • the inorganic or organic acid may be added in an amount of 0.1 to 20%, preferably 1 to 5%, based on water.
  • the exothermic agent for heating a smoker of the present invention can be used for any smoker conventionally used by heating by a direct heating method or an indirect heating method.
  • the ripening agent of the present invention can be combined with a conventional smoker to form a smoker kit.
  • the amount of the exothermic agent is 5 to 100% by weight, preferably 10 to 50% by weight, based on the total weight of the smoke agent. Good.
  • the amount of the exothermic agent is 20 to 100% by weight, preferably 50 to 200% by weight, based on the total weight of the smoke agent. It is good.
  • the exothermic agent and the smoker may not be in direct contact with each other but may be housed in different adjacent containers.
  • exothermic agent for heating a smoking agent of the present invention can be used for heating other than the smoking agent depending on the calorific value of the hydration reaction.
  • Example 1 Manufacturing method of exothermic agent for fumigation agent (granular)
  • Example 3 Manufacturing method of exothermic agent for heat generation of smoking agent (molded product without hole)
  • Example 4 Manufacturing method of exothermic agent for heat generation of smoking agent (molded product without hole)
  • Example 2 In the same manner as in Example 3, 0.4 g of the granular highly active calcium oxide of 1 to 5 mm in Example 1 was formed into a columnar shape having a tablet diameter ( ⁇ ) of 10 mm and a thickness of 5 mm. Comparative Example 1. Manufacturing method of exothermic agent for fumigation heat generation (perforated product)
  • Example 2 20 g of the highly active granular calcium oxide prepared in Example 1 was placed in a 0.27 mm glass tube, and at a temperature of 25 ° C, 6 ml of water was injected with a syringe to obtain calcium oxide. The internal maximum temperature was measured with a CA thermocouple located in the center, and the heating rate was calculated from the maximum temperature arrival time.
  • 20 g of granular calcium oxide of a reagent (manufactured by Wako Pure Chemical Industries) and a conventional product were measured in the same manner. Table 1 shows the results. Table 1 Maximum internal temperature and heat generation rate
  • the exothermic agent for heating the smoker of Example 2, Example 3 and Comparative Example 1 was 3 tablets each, and the exothermic agent for heating the smoker of Example 4 was 30 tablets, inner diameter 22 mm, height 5 It was inserted into an aluminum tube having a thickness of 0 mm and a thickness of 0.75 mm, and 4 ml of water or a 1% by weight aqueous solution of boric acid was added. Thereafter, the maximum surface temperature was measured by an infrared imaging device. Table 2 shows the results.
  • the actual heating test of the smoker was carried out by contacting the aluminum tubes of various calcium oxides conducted in Test Example 2 with 25 g of smoker granules.
  • Table 3 shows the results.
  • the formulation of the smoker granules is as follows,
  • the heat of hydration reaction of calcium oxide can be used not only for the indirect heating method for the smoke agent but also for the direct heating method.
  • the heating agent for heating the smoking agent of the present invention has a higher apparent specific gravity by tableting and molding, so that the heating agent for heating the smoking agent is smaller than the conventional container of the smoking agent using calcium oxide as the heating agent. Smaller and lighter containers can be made.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
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  • General Health & Medical Sciences (AREA)
  • Agronomy & Crop Science (AREA)
  • Pest Control & Pesticides (AREA)
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Abstract

A heat-generating agent for heating a fumigant, containing calcium oxide having a heat generation rate of at least 5 °C/sec when 20 g of calcium oxide and 6 ml of water are allowed to react with each other. A heating method of a fumigant comprising heating a fumigant by the heat generated when calcium oxide having a heat generation rate of at least 5 °C/sec and water are allowed to react with each other (when 20 g of calcium oxide and 6 ml of water are allowed to react). A heater for a fumigant, storing the heat-generating agent in a container and a fumigant kit including the heat-generating agent and the fumigant are also provided.

Description

明 細 書  Specification
燻煙剤加熱用発熱剤 技術分野 Exothermic agent for fumigation heating
本発明は、 高活性な酸化カルシゥムを含む燻煙剤加熱用発熱剤および高活性な 酸化カルシウムの水和反応により生じる熱を利用して燻煙剤を加熱する方法に関 する。 背景技術  The present invention relates to an exothermic agent for heating a smoke agent containing highly active calcium oxide and a method for heating the smoke agent using heat generated by a hydration reaction of calcium oxide with high activity. Background art
燻煙剤は、 有害生物駆除物質を加熱によって燻煙させる薬剤である。  Smoke-killers are agents that smoke pest control substances by heating.
従来、 燻煙剤を加熱し燻煙せしめる一つの方法としては、 ニ トロセルロース等 の自己燃焼性物質を含む燻煙剤を、 金属酸化物と珪素等との反応 (いわゆ テル ミ ッ ト反応) の発熱を利用し、 直接一挙に加熱 (点火) することにより、 燻煙剤 自身を自己燃焼させる直接加熱方法が知られている。 テルミ ッ ト反応による加熱 方法については、 実開昭 6 2— 1 4 6 4 2 7号および特開平 1— 2 8 8 2 1 8号 に開示されている。  Conventionally, as one method of heating and smoking a smoker, a smoker containing a self-combustible substance such as nitrocellulose is reacted with a metal oxide and silicon (a so-called thermite reaction). A direct heating method is known, in which the smoke is itself self-burned by directly heating (igniting) at once using the heat generated by the fumes. The heating method by the thermit reaction is disclosed in Japanese Utility Model Application Laid-Open No. 62-144627 and Japanese Patent Laid-Open No. 1-288218.
しカヽし、 テルミ ッ ト反応による加熱方法は、 燃焼反応によるものであることか ら、 加熱時に必要以上に高温となり、 そのため燻煙剤中の有効成分は熱分解を引 き起こす可能性があり、 熱分解性の高い薬剤を有効成分として使用するには問題 があった。  However, the heating method by thermite reaction is based on the combustion reaction, so the temperature rises more than necessary at the time of heating, so that the active ingredient in the smoke agent may cause thermal decomposition. However, there was a problem in using a highly thermally degradable drug as an active ingredient.
—方、 一般的に自己燃焼性を有さず、 いわゆる有機発泡剤を含む燻煙剤を、 多 量の酸化カルシウムと水との水和反応で発生する高熱により、 外部から間接的に、 比較的長時間穏やかに加熱する間接加熱方法もある (特公昭 5 9 — 4 9 2 0 1号) 上記間接加熱方法では、 酸化カルシウムを用いた水和反応の場合は酸化カルシ ゥム重量あたりの発熱量が低く、 このため殺虫成分を有効に揮散させるためには、 燻煙剤の重量よりもはるかに多くの重量の酸化カルシウムを必要とした。  On the other hand, smokers containing so-called organic blowing agents, which generally do not have self-combustibility, are compared indirectly from the outside due to the high heat generated by the hydration reaction between a large amount of calcium oxide and water. There is also an indirect heating method that heats gently for a long time (Japanese Patent Publication No. 59-49201). In the above-mentioned indirect heating method, in the case of a hydration reaction using calcium oxide, heat is generated per weight of calcium oxide. Because of its low volume, effective volatilization of the pesticidal components required much greater weight of calcium oxide than that of the smoke.
さらにまた、 間接加熱方法では、 多量の酸化カルシウムを用いても、 水を加え てからの発熱速度 (水和反応速度) が遅く、 燻煙が開始されるまでにかなりの時 _ 間を要した。 Furthermore, in the indirect heating method, even if a large amount of calcium oxide is used, the rate of heat generation after adding water (hydration reaction rate) is slow, and considerable time is required before smoking starts. _ It took time.
また、 実公平 5 - 6 9 2 2号では、 生石灰をリ ング状、 円筒状に打錠 ·成形し、 缶詰加熱用の加熱性発熱体として使用することが開示されている。 し力、し、 該加 熱用発熱体は、 単に、 容器に充塡しゃすく、 発熱剤の飛びちりを防ぎ、 缶詰を均 一に加熱することを目的にしているに過ぎず、 燻煙剤の燻煙を開始させるのに必 要な熱量を、 水添加後短時間で得るには不十分である。  Japanese Utility Model Publication No. 5-69922 discloses that quicklime is tableted and molded into a ring or a cylinder and used as a heating element for heating cans. The heating element is merely intended to fill the container, prevent the heating agent from flying off, and uniformly heat the can. The amount of heat required to initiate smoke in a short time after adding water is insufficient.
そこで、 本発明は、 上記の問題に鑑み、 有効成分の熱分解も少なく、 効率的に 燻煙剤を加熱せしめ、 速やかに燻煙を開始させるような、 酸化カルシウムを含む 燻煙剤加熱用発熱剤を提供することを目的とする。  In view of the above-mentioned problems, the present invention provides a heat generating apparatus for heating a smoking agent containing calcium oxide, which causes less thermal decomposition of the active ingredient, efficiently heats the smoking agent, and starts smoking immediately. It is intended to provide an agent.
さらに本発明は、 燻煙剤の間接加熱方法のみならず、 直接加熱方法にも使用で きるような、 酸化力ルシゥムを含む燻煙剤加熱用発熱剤を提供することも目的と する。 発明の開示  It is a further object of the present invention to provide a heating agent for heating a smoking agent containing oxidizing power, which can be used not only for an indirect heating method for a smoking agent but also for a direct heating method. Disclosure of the invention
本発明者は、 酸化カルシゥムの水和反応により発生する高熱を利用した燻煙剤 の加熱方法について鋭意検討を重ねた結果、 酸化カルシウム 2 0 gを水 6 mlと反 応させたときの発熱速度が 5 °C /秒以上の酸化カルシゥムを水和反応に付すこと により、 従来の酸化カルシウムの水和反応熱を利用する燻煙剤に比べ、 短時間で かつ少量の酸化カルシウムで、 燻煙剤を所望の温度にまで加熱することができる ことを明らかにした。  The present inventors have conducted intensive studies on a method of heating a smoke agent using high heat generated by a hydration reaction of calcium oxide, and as a result, the heat generation rate when 20 g of calcium oxide was reacted with 6 ml of water. Calcium oxide at a temperature of 5 ° C / sec or more is subjected to a hydration reaction. Can be heated to the desired temperature.
さらに、 上記の酸化カルシウムの成形体を使用することで、 酸化カルシウムの 水和反応熱を、 従来技術を用いた場合よりも、 時間で格段に高い温度に上昇さ せることに成功し、 この水和反応熱を燻煙剤の間接加熱方法のみならず直接加熱 方法にも利用できることを見出した。  Furthermore, by using the above-mentioned molded body of calcium oxide, it was possible to raise the heat of hydration reaction of calcium oxide to a much higher temperature in a time than in the case of using the conventional technology. We have found that the sum reaction heat can be used not only for the indirect heating method for smokers but also for the direct heating method.
また、 上記のような酸化カルシウムを打錠 '成形することで、 見かけ比重が高 くなることから、 従来の未成形の酸化カルシウムを発熱剤として使用した燻煙剤 の容器よりも、 小型化 ·軽量化された容器をつくることが可能となった。  In addition, since the apparent specific gravity is increased by tableting and molding calcium oxide as described above, the size is smaller than that of a conventional smoker container that uses unformed calcium oxide as a heating agent. It has become possible to make lightweight containers.
すなわち、 本発明は、 酸化カルシウム 2 0 gを水 6 mlと反応させたときの発熱 速度が 5 °CZ秒以上の酸化カルシウムを含む燻煙剤加熱用発熱剤を提供する。 本 発明の発熱剤は、 酸化カルシウムを水と反応させたときに発生する熱により、 発 熱剤の表面最高到達温度が加熱すべき燻煙剤の発煙温度以上になるように成形さ れているとよい。 その際の打錠圧力は、 2 0 0 ~ 4 0 0 kg/cm2が好ましい。 好ま しくは、 穴あき成形体の形状に打錠成形されるとよい。 穴あき成形体の形状とし ては、 円筒状、 リング状、 カップ状などを挙げることができる。 That is, the present invention provides a heating agent for heating a smoking agent containing calcium oxide having a heat generation rate of 5 ° CZ seconds or more when 20 g of calcium oxide is reacted with 6 ml of water. Book The exothermic agent of the invention is shaped so that the maximum temperature of the surface of the exothermic agent is equal to or higher than the fuming temperature of the smoking agent to be heated by heat generated when calcium oxide is reacted with water. Good. The tableting pressure at that time is preferably from 200 to 400 kg / cm 2 . Preferably, it is tablet-formed into a shape of a perforated molded body. Examples of the shape of the perforated molded body include a cylindrical shape, a ring shape, and a cup shape.
また、 本発明は、 発熱速度が 5 °CZ秒以上 (酸化カルシウム 2 0 gを水 6 mlと 反応させたとき) の酸化カルシウムを水と反応させたときに発生する熱により燻 煙剤を加熱することを特徴とする、 燻煙剤の加熱方法を提供する。 加熱すべき燻 煙剤の全重量を基準として 1 0 0重量%以下の酸化カルシウムを水と反応させる とよい。 好ましくは、 無機酸および Zまたは有機酸の存在下で、 酸化カルシウム を水と反応させるとよい。  The present invention also provides a method for heating a smoking agent by heat generated when calcium oxide having a heat generation rate of 5 ° CZ seconds or more (when 20 g of calcium oxide is reacted with 6 ml of water) is reacted with water. And a method for heating a smoking agent. Less than 100% by weight of calcium oxide, based on the total weight of the smoke agent to be heated, may be reacted with water. Preferably, calcium oxide is reacted with water in the presence of an inorganic acid and Z or an organic acid.
燻煙剤に使用することができる薬剤としては, 目的に応じ殺虫剤、 殺菌斉 I] ^の 各種薬剤ならびにそれらの混合剤が挙げられる。  Drugs that can be used as fumigation agents include insecticides, various germicides I] ^ and their mixtures according to the purpose.
上記の殺虫剤としては、 例えば、 ペルメ トリ ン、 アレスリ ン、 レスメ トリ ン、 サイフエノ ト リ ン、 プラレスリ ン、 フヱノ ト リ ン、 フヱンバレレー ト、 フェンプ ロノ、 ° ト リ ン、 エトフエンプロックス等のピレスロイ ド系薬剤、 フエニトロチオン、 ジクロルボス (D D V P ) 、 ダイアジノ ン、 プロチォホス、 バイテックス等の有 機リン系薬剤、 プロポクスル、 メ トキサジァゾン等のカーバメイ ト系薬剤等が使 用できる。  Examples of the above insecticides include, for example, pyrethroids such as permethrin, allesulin, resmethrin, cyphenothrin, pralethrin, phenothrin, humvalerate, fenprono, ° trin, etofenprox, etc. Organic drugs, such as organic compounds, phennitrothion, dichlorvos (DDVP), diazinon, protifos, and vitex, and carbamates such as propoxur and methoxadiazon.
上記の殺菌剤としては、 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 —ョード 2 —プロピニルブ チルカーバメート ( I P B C ) 、 I F— 1 0 0 0等の環境衛生用殺菌剤等が使用 できる。  Examples of the above-mentioned fungicides include fungicides for agricultural chemicals such as isophthalonitrile, procymidone, biletone, and molestan, thiabendazole, 3-odo-2—propynylbutyl carbamate (IPBC), IF-100, etc. Environmental sanitizing germicides can be used.
上記の薬剤の含有量は、 燻煙剤の全重量を基準として、 2重量%以上 2 0重量 %以下が好ましい。  The content of the above drug is preferably 2% by weight or more and 20% by weight or less based on the total weight of the smoking agent.
本発明の加熱方法は、 直接加熱方法で加熱される燻煙剤および間接加熱方法で 加熱される燻煙剤のいずれに対しても利用することができる。 燻煙剤用燃焼基剤 として、 ニトロセルロース、 ァゾジカルボンア ミ ド、 ジニトロソペンタメチレン テ トラ ミ ン、 ォキシビスベンゼンスルフォニルヒ ドラジ ド、 ニ トログァニジン、 ならびに塩素酸力リゥムゃ硝酸ァンモニゥム等の酸化剤と糖類や木粉等の可燃性 物質からなる組成物等が挙げられる。 かかる燻煙剤は、 上記の薬剤、 燻煙剤用発 熱剤の他、 メラ ミ ン、 酸化亜鉛などの発熱助剤、 ク レー、 カオリ ン、 タルク、 珪 藻土などの無機系鉱物質の添加も可能である。 更に、 カルボキンメチルセル口一 ス、 ヒ ドロキンプロピルメチルセルロース、 ポリ ビニルアルコール、 でんぷんな どの結合剤や香料、 ピぺロニルブトキサイ ド、 S— 4 2 1等の効力増強剤、 B H T、 トコフヱロールなどの酸化防止剤といった添加剤等を含有してもよい。 直接 加熱方法で加熱される燻煙剤および間接加熱方法で加熱される燻煙剤のいずれで あっても、 粉剤、 顆粒剤、 錠剤、 ペースト剤などの剤型であるとよい。 The heating method of the present invention can be used for both smokers heated by the direct heating method and smokers heated by the indirect heating method. Nitrocellulose, azodicarbonamide, dinitrosopentamethylene tetramamine, oxybisbenzenesulfonyl hydrazide, nitroguanidine, And a composition comprising an oxidizing agent such as chloric acid-containing realm and ammonium nitrate and a combustible substance such as sugars and wood flour. Such fumigation agents include the above-mentioned chemicals, heat generation agents for fumigation agents, heat-generating aids such as melamine and zinc oxide, and inorganic minerals such as clay, kaolin, talc, and diatomaceous earth. Addition is also possible. Furthermore, binders and fragrances such as carboquine methylcellulose, hydroxyquinepropyl methylcellulose, polyvinyl alcohol, starch, potency enhancers such as piperonyl butoxide, S-421, and oxidation of BHT, tocoprole, etc. An additive such as an inhibitor may be contained. Both smokers heated by the direct heating method and smokers heated by the indirect heating method are preferably in the form of powders, granules, tablets, pastes and the like.
さらに、 本発明は、 上記の発熱剤を容器に収納した燻煙剤加熱装置を提供する 容器は、 水和反応等で発生した熱量を効率的に該容器に接する燻煙剤に伝えるこ とができるものであるとよい。 例えば、 好ましくは、 5 W/m ' °C以上、 より好 ましくは、 1 0 WZm · °C以上の熱伝導率 (2 5 °Cの場合) を有する容器がよい c かかる容器としては、 アルミニウム、 ブリキ、 銅、 鉄等から選択される材料で製 造されているものを挙げることができる。 さらに、 容器は密封されているとよい c さらにまた、 本発明は、 上記の発熱剤および燻煙剤を含む燻煙剤キッ トを提供 する。 燻煙剤は、 前記のような、 直接加熱方法で加熱される燻煙剤または間接加 熱方法で加熱される燻煙剤のいずれであってもよい。 Further, the present invention provides a smoker heating device in which the above-mentioned exothermic agent is housed in a container, wherein the container is capable of efficiently transmitting heat generated by a hydration reaction or the like to the smoker in contact with the container. It should be something you can do. For example, preferably, 5 W / m '° C or higher, more favorable Mashiku as container according good c container having a 1 0 WZm · ° C or more heat conductivity (the case of 2 5 ° C), Examples include those made of a material selected from aluminum, tin, copper, iron, and the like. Further, the container further when it c being sealed Further, the present invention provides a fumigant kit containing the above-described heating agent and smoking agents. The smoker may be either a smoker heated by a direct heating method or a smoker heated by an indirect heating method as described above.
本明細書において、 「発熱速度」 とは、 酸化カルシウムと水との水和反応によ る発熱の開始時間から最高温度到達時間までの、 1秒あたりの平均上昇温度を示 す。 発熱速度は、 2 5 °Cまたは室温で、 ガラス管に酸化カルシウムの粉状品また は粒状品を 2 O g入れ、 水 6 mlと水和反応させ、'酸化カルシウム中央に配した C A熱電対により内部最高温度を測定し、 水和反応開始から最高温度到達までの、 1秒あたりの平均上昇温度を求めることにより、 決定することができる。  In the present specification, the “heat generation rate” indicates an average temperature increase per second from the start time of heat generation by the hydration reaction of calcium oxide and water to the time to reach the maximum temperature. The heat generation rate is 25 ° C or room temperature.Powder or granules of calcium oxide are placed in a glass tube at 2 Og, and hydrated with 6 ml of water. Can be determined by measuring the maximum internal temperature and calculating the average temperature rise per second from the start of the hydration reaction to the maximum temperature.
従来の、 燻煙剤の加熱に用いられている酸化カルシウムの発熱速度は、 酸化力 ルシゥム 2 0 gを水 6 mlと反応させたとき、 3 ノ秒程度以下である。 一方、 本 発明に用いる酸化カルシウムの発熱速度は、 酸化カルシウム 2 0 gを水 6 mlと反 応させたとき、 5 °CZ秒以上であり、 好ましくは 6 °CZ秒以上である。 本発明に 用いる、 酸化カルシウム 2 0 gを水 6 mlと反応させたときの発熱速度が 5 °C/秒 以上の酸化カルシウムを、 以下、 「高活性な酸化カルシウム」 と称することとす 本発明における 「穴あき成形体」 とは、 1個ないし 2個以上の穴を有した、 円 柱状、 立方体状、 直方体、 多角形柱状、 多角形体、 球状等の成形体を言い、 その 穴は、 該成形体を貫通していてもよいし、 貫通していなくてもよい。 穴が貫通し ていない場合、 その穴の深さは、 該成形体の厚さの 1 / 3以上であることが望ま しい。 The heat generation rate of calcium oxide, which has been conventionally used for heating a smoking agent, is about 3 ns or less when 20 g of oxidizing power is reacted with 6 ml of water. On the other hand, the heat generation rate of calcium oxide used in the present invention is at least 5 ° CZ seconds, preferably at least 6 ° CZ seconds when 20 g of calcium oxide is reacted with 6 ml of water. The heat generation rate when reacting 20 g of calcium oxide with 6 ml of water used in the present invention is 5 ° C / sec. The above calcium oxide is hereinafter referred to as “highly active calcium oxide”. The “perforated molded body” in the present invention is a columnar, cubic, It refers to a molded article such as a rectangular parallelepiped, polygonal column, polygon, or sphere, and the hole may or may not penetrate the molded article. When the hole does not penetrate, it is desirable that the depth of the hole is not less than 1/3 of the thickness of the molded body.
このような穴あき成形体としては、 例えば、 円筒状、 リ ング状、 カップ状等の 成形体が挙げられる。  Examples of such a perforated formed body include a formed body having a cylindrical shape, a ring shape, a cup shape, and the like.
また、 該穴あき成形体の代わりに、 高活性な酸化カルシウムを、 成形体の表面 に溝を切ったり、 成形体を星形等にするなどして、 打錠成形することによって、 酸化カルシゥム単位重量あたりの表面積が、 該穴あき成形体と同程度とな 形 体も、 本発明の穴あき成形体と同様の効果を得ることができる。 発明を実施するための最良の形態  In addition, instead of the perforated molded body, highly active calcium oxide is cut into grooves on the surface of the molded body, or the molded body is formed into a star shape or the like, and is subjected to tablet compression molding to form calcium oxide units. A shape having a surface area per weight equivalent to that of the perforated molded article can also obtain the same effect as the perforated molded article of the present invention. BEST MODE FOR CARRYING OUT THE INVENTION
まず、 高活性な酸化カルシウムを用意する。 高活性な酸化カルシウムは、 例え ば、 消石灰を、 実質的に二酸化炭素が存在しない条件下で、 1 0分〜 6時間程度、 5 5 0〜7 7 0 °Cに加熱して脱水させる方法等により製造することができる (特 開平 1 — 3 0 8 8 2 5号を参照のこと) 。  First, prepare highly active calcium oxide. Highly active calcium oxide is, for example, a method of dehydrating slaked lime by heating it to 550 to 770 ° C for about 10 minutes to 6 hours under conditions substantially free of carbon dioxide. (See Japanese Patent Application Publication No. 1-3088885).
燻煙剤加熱用発熱剤として使用するにあたっては、 上記の方法で製造した高活 性な酸化カルシウムの粉粒体をそのまま使用してもよいが、 好ましくは、 常法に より打錠し、 円筒状、 リング状、 コップ状等に成形する。  When used as an exothermic agent for heating a smoking agent, the powdered granules of highly active calcium oxide produced by the above method may be used as they are, but preferably, they are compressed into tablets by a conventional method, and Into a ring, ring, cup, etc.
このときの打錠圧は、 2 0 0〜4 0 0 kg/cm2が好ましい。 打錠圧が、 2 0 0 kg /cm2未満では良好な成形物が得難く、 4 0 0 kg/cm2をこえると成形体にひび割れ が生じる可能性がある。 The tableting pressure at this time is preferably from 200 to 400 kg / cm 2 . If the tableting pressure is less than 200 kg / cm 2, it is difficult to obtain a good molded product, and if it exceeds 400 kg / cm 2 , cracks may occur in the molded product.
成形は、 高活性な酸化カルシウムのみを打錠しても良好であるが、 ステアリン 酸マグネシウム、 ステアリン酸カルシウム、 タルク、 ラウリル硫酸ナトリウムな どの滑沢剤を使用することで、 さらに打錠成形性を向上することができる。  It is good to mold only highly active calcium oxide for tableting, but using a lubricant such as magnesium stearate, calcium stearate, talc, or sodium lauryl sulfate further improves tableting moldability. can do.
このときの錠剤径 (ø ) および穴径 (ø ) の寸法は特に規定はなく、 使用目的、 希望する発熱量、 収納容器の大きさ等に合わせて決めればよい。 At this time, the dimensions of the tablet diameter (ø) and hole diameter (ø) are not particularly specified. It may be determined according to the desired calorific value and the size of the storage container.
本発明の穴あき成形体を作成する場合、 打錠径 (ø 1 ) と穴径 (ø 2 ) の比 ( ø 2 Z 0 1 ) は、 0 . 1〜 0 . 8、 好ましくは 0 . 2〜 0 . 5である。  When the perforated molded body of the present invention is prepared, the ratio (ø2Z01) of the tableting diameter (ø1) to the hole diameter (ø2) is 0.1 to 0.8, preferably 0.2. ~ 0.5.
このときの成形品の 1個あたりの重量は希望する発熱量によって異なるが、 一 般に 1〜 2 4 g、 好ましくは 2〜 1 5 gである。 また、 本発明の燻煙剤加熱用発 熱剤は、 単独で使用することもできるし、 複数個を積み重ねるなどして使用する こともできる。  At this time, the weight of each molded article varies depending on the desired calorific value, but is generally 1 to 24 g, preferably 2 to 15 g. Further, the heat generating agent for heating a smoking agent of the present invention can be used alone, or can be used by stacking a plurality of them.
本発明の燻煙剤加熱用発熱剤は、 従来の燻煙剤加熱用の酸化カルシウムが、 燻 煙剤を加熱、 発煙させるために、 燻煙剤よりもはるかに多い重量を必要としたの に対し、 燻煙剤の重量よりも少ない酸化カルシウム重量で燻煙剤を加熱し、 発煙 させることができる。  The heating agent for heating the smoker of the present invention requires much more weight than the conventional smoker for heating and smoking the calcium oxide for heating the smoker. On the other hand, the smoker can be heated and smoked with a smaller weight of calcium oxide than the smoker.
さらに、 本発明の燻煙剤用発熱剤は、 打錠することにより、 見かけ比重カ く なり、 従来よりも少量の加熱用スペースでの容器形態を設計することが可能とな り、 従来より小型化 ·軽量化された燻煙剤容器を設計することが可能となる。 例えば、 本発明の燻煙剤加熱用発熱剤を、 アルミ製、 ブリキ製、 銅製、 鉄製等 の熱伝導性の高い容器に密封することにより、 小型化 ·軽量化された燻煙剤の加 熱装置を作ることができる。  Furthermore, the exothermic agent for smokers of the present invention becomes apparently more specific by tableting, and it is possible to design a container form with a smaller heating space than before, and it is possible to make it smaller than before.・ It is possible to design a smoker container that is lighter. For example, the exothermic agent for heating the smoking agent of the present invention is sealed in a highly heat-conductive container made of aluminum, tin, copper, iron, or the like, so that the heating of the smoking agent, which has been reduced in size and weight, can be performed. Equipment can be made.
従来、 酸化カルシウムによる燻煙剤の加熱方法は、 燻煙剤を収納している容器 の外側から燻煙剤を加熱していたのに対し、 上記の燻煙剤の加熱装置を用いるこ とにより、 燻煙剤を収納している容器の内部に加熱装置を設置して燻煙剤を加熱 する方式の燻煙剤容器を設計することが可能となり、 従来より小型化 ·軽量化さ れた燻煙剤用器を設計することが実現できる。 '  Conventionally, the method of heating a smoke agent with calcium oxide has been to heat the smoke agent from the outside of the container containing the smoke agent. In addition, it is possible to design a smoker container that heats the smoker by installing a heating device inside the container that holds the smoker, making the smoker smaller and lighter than before. It is feasible to design a smoke agent vessel. '
また、 上記の加熱装置は、 テルミ ッ ト反応の反応熱を利用した点火装置の代わ りに、 自己燃焼性物質を含む燻煙剤を直接加熱するための点火装置としても使用 することができる。 該加熱装置を使用することにより、 テルミ ッ ト反応の反応熱 による点火に比べ、 燻煙剤の点火時における有効成分の熱分解を抑えることがで きる。  In addition, the above-described heating device can be used as an ignition device for directly heating a smoking agent containing a self-combustible substance, instead of an ignition device using reaction heat of a thermite reaction. By using the heating device, it is possible to suppress the thermal decomposition of the active ingredient at the time of ignition of the smoking agent, as compared with the ignition by the reaction heat of the thermite reaction.
また、 本発明の燻煙剤加熱用発熱剤を使用する際には、 水のみと水和反応させ ても、 燻煙剤の加熱は良好であるが、 無機酸および または有機酸の存在下で、 水和反応を行うことで、 さらに効率的に燻煙剤を加熱させ、 燻煙を開始するまで の時間を調節することができる。 酸を添加することにより、 表面最高到達温度が さらに上昇する。 In addition, when using the exothermic agent for heating the smoking agent of the present invention, the heating of the smoking agent is good even if the hydration reaction is performed with only water, but in the presence of an inorganic acid and / or an organic acid. , By performing the hydration reaction, the smoker can be heated more efficiently, and the time until smoke starts can be adjusted. The addition of the acid further increases the maximum surface temperature.
無機酸としては、 例えば、 ホウ酸、 硝酸、 塩酸、 過塩素酸等が挙げられる。 ま た、 有機酸としては、 例えば、 コハク酸、 シユウ酸、 リ ンゴ酸、 ァスコルビン酸、 クェン酸等が挙げられる。  Examples of the inorganic acid include boric acid, nitric acid, hydrochloric acid, perchloric acid and the like. In addition, examples of the organic acid include succinic acid, oxalic acid, lingic acid, ascorbic acid, and citric acid.
高活性な酸化カルシウムと反応させる水は化学量論比土 0 . 5となる量で添加 するとよい。 また、 無機酸または有機酸は、 水に対して 0 . 1 ~ 2 0 %、 好まし くは 1〜 5 %の量で添加するとよい。  It is advisable to add water to be reacted with highly active calcium oxide in such an amount that the stoichiometric ratio is 0.5. The inorganic or organic acid may be added in an amount of 0.1 to 20%, preferably 1 to 5%, based on water.
本発明の燻煙剤加熱用発熱剤は、 従来より直接加熱方法あるいは間接加熱方法 により加熱して使用される、 いかなる燻煙剤に対しても使用できる。  The exothermic agent for heating a smoker of the present invention can be used for any smoker conventionally used by heating by a direct heating method or an indirect heating method.
本発明の発熟剤を従来の燻煙剤と組み合わせて、 燻煙剤キッ 卜にすること で きる。 直接加熱方法で加熱される燻煙剤と組み合わせる場合には、 発熱剤の量は 燻煙剤の全重量を基準として 5〜 1 0 0重量%、 好ましくは 1 0〜 5 0重量%で あるとよい。 間接加熱方法で加熱される燻煙剤と組み合わせる場合には、 発熱剤 の量は燻煙剤の全重量を基準として 2 0〜 1 0 0 0重量%、 好ましくは 5 0〜 2 0 0重量%であるとよい。  The ripening agent of the present invention can be combined with a conventional smoker to form a smoker kit. When combined with a smoke agent heated by a direct heating method, the amount of the exothermic agent is 5 to 100% by weight, preferably 10 to 50% by weight, based on the total weight of the smoke agent. Good. When combined with a smoke agent heated by the indirect heating method, the amount of the exothermic agent is 20 to 100% by weight, preferably 50 to 200% by weight, based on the total weight of the smoke agent. It is good.
本発明の燻煙剤キッ トにおいて、 発熱剤と燻煙剤は、 直接接するのではなく、 隣接する異なる容器に収納されるとよい。  In the smoker kit of the present invention, the exothermic agent and the smoker may not be in direct contact with each other but may be housed in different adjacent containers.
また、 本発明の燻煙剤加熱用発熱剤は、 水和反応の発熱量に応じて、 燻煙剤以 外の加熱にも使用できる。  Further, the exothermic agent for heating a smoking agent of the present invention can be used for heating other than the smoking agent depending on the calorific value of the hydration reaction.
以下に、 実施例によって本発明を具体的に説明するが、 本発明の範囲はこれら に限定されるものではない。 実施例 1 . 燻煙剤発熱用発熱剤の製法 (粒状)  Hereinafter, the present invention will be described specifically with reference to Examples, but the scope of the present invention is not limited thereto. Example 1 Manufacturing method of exothermic agent for fumigation agent (granular)
特開平 1 一 3 0 8 8 2 5号に記載の方法に従って、 消石灰を、 実質的に二酸化 炭素が存在しない条件下で、 約 4時間、 6 0 0 °Cに加熱して脱水させて、 1〜5 画の粒状の高活性酸化カルシゥムを得た。 -W 実施例 2 . 燻煙剤発熱用発熱剤の製法 (穴あき成形品) According to the method described in Japanese Patent Application Laid-Open Publication No. Hei 13-80825, slaked lime was heated at 600 ° C. for about 4 hours under a condition substantially free of carbon dioxide to dehydrate it. ~ 5 fractions of granular highly active calcium oxide were obtained. -W Example 2. Production method of exothermic agent for fumigation heat generation (perforated molded product)
実施例 1の 1 〜 5 mmの粒状の高活性酸化カルシウム 4 gを、 打錠圧 2 4 0 kg/c m2で打錠し、 錠剤径 (ø ) 2 0 mm、 穴径 ø 6 . 3 誦、 厚さ 1 2 mmの円筒状に成形 した。 このとき打錠成形時に、 打錠成形性をよくする為に、 ステアリン酸マグネ シゥム少量を金型表面に添加した。 実施例 3 . 燻煙剤発熱用発熱剤の製法 (穴なし成形品) 4 g of 1-5 mm granular high-activity calcium oxide of Example 1 was tableted at a tableting pressure of 240 kg / cm 2 , tablet diameter (ø) 20 mm, hole diameter ø 6.3. It was formed into a cylinder having a thickness of 12 mm. At this time, a small amount of magnesium stearate was added to the surface of the mold to improve the tableting formability during tableting. Example 3. Manufacturing method of exothermic agent for heat generation of smoking agent (molded product without hole)
実施例 1の 1 〜 5 mmの粒状の高活性酸化カルシウム 4 . 2 gを、 打錠圧 2 4 0 kg/cm2で打錠し、 錠剤径 (ø ) 2 O mm、 厚さ 1 2画の円柱状に成形した。 このと き打錠成形時に、 実施例 2と同様に、 ステアリン酸マグネシウム少量を金型に添 加した。 実施例 4 . 燻煙剤発熱用発熱剤の製法 (穴なし成形品) 4.2 g of 1-5 mm granular highly active calcium oxide of Example 1 was tableted at a tableting pressure of 240 kg / cm 2 , with a tablet diameter (ø) 2 O mm and a thickness of 12 strokes. Into a cylindrical shape. At this time, a small amount of magnesium stearate was added to the mold at the time of tableting as in Example 2. Example 4. Manufacturing method of exothermic agent for heat generation of smoking agent (molded product without hole)
実施例 3と同様にして、 実施例 1の 1 〜 5 mmの粒状の高活性酸化カルシウム 0 . 4 gを、 錠剤径 (ø ) 1 0 mm, 厚さ 5 mmの円柱状に成形した。 比較例 1 . 燻煙剤発熱用発熱剤の製法 (穴あき成形品)  In the same manner as in Example 3, 0.4 g of the granular highly active calcium oxide of 1 to 5 mm in Example 1 was formed into a columnar shape having a tablet diameter (ø) of 10 mm and a thickness of 5 mm. Comparative Example 1. Manufacturing method of exothermic agent for fumigation heat generation (perforated product)
1 〜 5 顏の粒状の市販の酸化カルシウム (和光純薬製) 4 gを、 実施例 2と同 様にして円筒状に成形した。 試験例 1 . 発熱速度  In the same manner as in Example 2, 4 g of granular commercially available calcium oxide (manufactured by Wako Pure Chemical Industries, Ltd.) of 1 to 5 faces was formed into a cylindrical shape. Test example 1. Heat generation rate
実施例 1で調製した粒状の高活性な酸化カルシウム 2 0 gを、 0 2 7 mmのガラ ス管に入れ、 2 5 °Cの温度下で、 水 6 mlをシリ ンジで注入し、 酸化カルシウム中 央に配した C A熱電対により内部最高温度を測定し、 最高温度到達時間から昇温 速度を算出した。 なお、 比較例として、 試薬用 (和光純薬製) および従来品の粒 状の酸化カルシウム 2 0 gを同様に測定した。 その結果を第 1表に示す。 第 1表 内部最高温度及び発熱速度 20 g of the highly active granular calcium oxide prepared in Example 1 was placed in a 0.27 mm glass tube, and at a temperature of 25 ° C, 6 ml of water was injected with a syringe to obtain calcium oxide. The internal maximum temperature was measured with a CA thermocouple located in the center, and the heating rate was calculated from the maximum temperature arrival time. As a comparative example, 20 g of granular calcium oxide of a reagent (manufactured by Wako Pure Chemical Industries) and a conventional product were measured in the same manner. Table 1 shows the results. Table 1 Maximum internal temperature and heat generation rate
;化カルシウム 性状 内部最高温度 (°c ) 発熱速度 (°CZ秒) 実施例 1 3 2 2 7 . 1 ; Calcium iodide property Maximum internal temperature (° C) Heat release rate (° CZ seconds) Example 13 22 7.
試薬用 状状状 6 0 0 . 6  Reagent form 600 .6
従 1?:ロロ 2 3 6 3 . 1  Obey 1 ?: Loro 2 3 6 3. 1
試験例 2 . 表面最高温度 Test example 2. Maximum surface temperature
実施例 2、 実施例 3ならびに比較例 1の、 燻煙剤加熱用発熱剤を 3錠ずつ、 実 施例 4の燻煙剤加熱用発熱剤を 3 0錠、 内径 2 2 mm、 高さ 5 0 mm、 厚さ 0 . 7 5 mmのアルミ管に挿入し、 水あるいは 1重量%ホウ酸水溶液 4 m 1を添加し、 その 後の表面最高到達温度を赤外線映像装置により測定した。 その結果を第 2表に示 す。  The exothermic agent for heating the smoker of Example 2, Example 3 and Comparative Example 1 was 3 tablets each, and the exothermic agent for heating the smoker of Example 4 was 30 tablets, inner diameter 22 mm, height 5 It was inserted into an aluminum tube having a thickness of 0 mm and a thickness of 0.75 mm, and 4 ml of water or a 1% by weight aqueous solution of boric acid was added. Thereafter, the maximum surface temperature was measured by an infrared imaging device. Table 2 shows the results.
第 2表 表面最高到達温度測定結果 酸化カルシゥム 性状 酸 表面最高到達温度 (°C) 実施例 2 穴あき成形品 無添加 (水) 2 3 3  Table 2 Results of measurement of maximum surface temperature Temperature of calcium oxide Properties Acid Maximum surface temperature (° C) Example 2 Perforated molded product No additive (water) 2 3 3
実施例 2 穴あき成形品 ホウ酸 2 5 0  Example 2 Perforated molded product Boric acid 250
実施例 3 穴なし成形品 無添加 (水) ' 7 6  Example 3 Molded product without holes No additive (water) '7 6
実施例 4 穴なし成形品 無添加 (水) 2 2 1  Example 4 Molded product without holes No additive (water) 2 2 1
比較例 1 穴あき成形品 無添加 (水) 4 2  Comparative Example 1 Perforated molded product No additive (water) 4 2
試験例 3 . 加熱発煙試験 Test example 3. Heat and smoke test
実際の燻煙剤の加熱試験を、 試験例 2で行つた各種酸化カルシウムの人ったァ ルミ管を、 燻煙剤顆粒 2 5 gと接触させて行った。 結果を第 3表に示す。 なお、 燻煙剤顆粒の処方は以下のとおりである, The actual heating test of the smoker was carried out by contacting the aluminum tubes of various calcium oxides conducted in Test Example 2 with 25 g of smoker granules. Table 3 shows the results. The formulation of the smoker granules is as follows,
メ トキサジァゾン 5 %  Methoxadiazone 5%
フエノ ト リ ン 2 %  Phenotrin 2%
ァゾジカルボンァミ ド 4 0 %  Azodicarbonamide 40%
二 ト ロセノレロース 1 0 %  2 Torosenorelose 10%
カルボキシメチルセルロース 5 %  Carboxymethyl cellulose 5%
ク レー  Cray
全量 1 0 0 % 第 3表 加熱発煙試験結果 酸化カルシゥム 性状 酸 発煙の有無 実施例 2 穴あき成形品 無添加 (水) 発煙有  Total amount 100% Table 3 Results of Heating and Smoke Tests Calcium Oxide Properties Acid Smoke Existence Example 2 Perforated Molded Product No Addition (Water)
実施例 2 穴あき成形品 ホウ酸  Example 2 Perforated molded product Boric acid
実施例 3 穴なし成形品 無添加 (水) 発煙無  Example 3 Molded product without holes No additive (water) No fuming
実施例 4 穴なし成形品 無添加 (水)  Example 4 Molded product without holes No additive (water)
比較例 1 穴あき成形品 無添加 (水) 発煙  Comparative Example 1 Perforated molded article No additive (water) fuming
産業上の利用の可能性 Industrial applicability
本発明により、 従来の酸化カルシゥムの水和反応熱を利用した燻煙剤に比べ、 短時間で、 かつ少量の酸化カルシウムで、 燻煙剤を所望の温度にまで加熱するこ とができるようになった。  According to the present invention, it is possible to heat a smoker to a desired temperature in a short time and with a small amount of calcium oxide, as compared with a conventional smoker utilizing heat of hydration reaction of calcium oxide. became.
さらに、 本発明の燻煙剤加熱用発熱剤を使用することで、 酸化カルシウムの水 和反応熱を、 燻煙剤の間接加熱方法のみならず直接加熱方法にも使用できる。 また、 本発明の燻煙剤加熱用発熱剤は、 打錠 ·成形することで、 見かけ比重が 高くなることから、 従来の、 酸化カルシウムを発熱剤として使用した燻煙剤の容 器よりも、 小型化 ·軽量化された容器をつくることが可能となった。  Further, by using the exothermic agent for heating the smoking agent of the present invention, the heat of hydration reaction of calcium oxide can be used not only for the indirect heating method for the smoke agent but also for the direct heating method. In addition, the heating agent for heating the smoking agent of the present invention has a higher apparent specific gravity by tableting and molding, so that the heating agent for heating the smoking agent is smaller than the conventional container of the smoking agent using calcium oxide as the heating agent. Smaller and lighter containers can be made.

Claims

請 求 の 範 囲. The scope of the claims.
1 . 酸化カルシウム 2 0 gを水 6 mlと反応させたときの発熱速度が 5 °CZ秒以上 の酸化カルシゥムを含む燻煙剤加熱用発熱剤。 1. An exothermic agent for heating a smoking agent containing calcium oxide, which has a heating rate of 5 ° CZ seconds or more when 20 g of calcium oxide is reacted with 6 ml of water.
2 . 酸化カルシウムを水と反応させたときに発生する熱により、 発熱剤の表面最 高到達温度が加熱すべき燻煙剤の発煙温度以上になるように成形されている請求 の範囲第 1項記載の発熱剤。  2. The heat-generating agent is formed such that the maximum surface temperature of the heating agent is equal to or higher than the fuming temperature of the smoking agent to be heated by heat generated when the calcium oxide is reacted with water. The exothermic agent as described.
3 . 2 0 0〜4 0 0 kg/cm2の打錠圧力で成形されている請求の範囲第 1項または 第 2項記載の発熱剤。 3. The exothermic agent according to claim 1 or 2, wherein the exothermic agent is formed at a compression pressure of 3.2 to 400 kg / cm 2 .
4 . 穴あき成形体の形状に打錠成形されている請求の範囲第 1項または第 2項記 載の発熱剤。  4. The exothermic agent according to claim 1 or 2, wherein the exothermic agent is tablet-formed into a perforated molded article.
5 . 穴あき成形体の形状が、 円筒状、 リング状またはカップ状のいずれかで:^る 請求の範囲第 4項記載の発熱剤。  5. The exothermic agent according to claim 4, wherein the shape of the perforated formed body is any one of a cylindrical shape, a ring shape, and a cup shape.
6 . 発熱速度が 5 CZ秒以上 (酸化カルシウム 2 0 gを水 6 miと反応させたとき) の酸化カルシウムを水と反応させたときに発生する熱により燻煙剤を加熱するこ とを特徴とする、 燻煙剤の加熱方法。  6. The fumigation agent is heated by the heat generated when calcium oxide having a heat generation rate of 5 CZ seconds or more (when 20 g of calcium oxide is reacted with 6 mi of water) is reacted with water. The method of heating the smoker.
7 . 加熱すべき燻煙剤の全重量を基準として i 0 0重量%以下の酸化カルシウム を水と反応させる請求の範囲第 6項記載の方法。  7. The method according to claim 6, wherein less than 100% by weight of calcium oxide is reacted with water, based on the total weight of the smoking agent to be heated.
8 . 無機酸および/または有機酸の存在下で、 酸化カルシウムを水と反応させる 請求の範囲第 6項または第 7項に記載の方法。  8. The method according to claim 6 or 7, wherein the calcium oxide is reacted with water in the presence of an inorganic acid and / or an organic acid.
9 . 請求の範囲第 1項〜第 5項のいずれかに記載の発熱剤を容器に収納した燻煙 剤加熱装置。  9. A smoker heating device containing the exothermic agent according to any one of claims 1 to 5 in a container.
1 0 . 容器が 5 WZm · °C以上の熱伝導率 (2 5 °Cの場合) を有するものである 請求の範囲第 9項記載の装置。  10. The apparatus according to claim 9, wherein the container has a thermal conductivity of 5 WZm · ° C or more (at 25 ° C).
1 1 . 容器が、 アルミニウム、 ブリキ、 銅および鉄からなる群より選択される材 料で製造されている請求の範囲第 1 0項記載の装置。  11. The apparatus according to claim 10, wherein the container is made of a material selected from the group consisting of aluminum, tin, copper and iron.
PCT/JP1998/000637 1997-02-17 1998-02-17 Heat-generating agent for heating fumigant WO1998035552A1 (en)

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Cited By (11)

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WO2000042117A1 (en) * 1999-01-14 2000-07-20 Earth Chemical Co., Ltd. Heat transpiration preparation and method of the heat transpiration of chemical by using the same
US10036574B2 (en) 2013-06-28 2018-07-31 British American Tobacco (Investments) Limited Devices comprising a heat source material and activation chambers for the same
US10542777B2 (en) 2014-06-27 2020-01-28 British American Tobacco (Investments) Limited Apparatus for heating or cooling a material contained therein
US11064725B2 (en) 2015-08-31 2021-07-20 British American Tobacco (Investments) Limited Material for use with apparatus for heating smokable material
US11241042B2 (en) 2012-09-25 2022-02-08 Nicoventures Trading Limited Heating smokeable material
WO2022184946A1 (en) * 2021-03-02 2022-09-09 Global Termobiomasa S.L. Multipurpose autonomous thermal device
US11452313B2 (en) 2015-10-30 2022-09-27 Nicoventures Trading Limited Apparatus for heating smokable material
US11659863B2 (en) 2015-08-31 2023-05-30 Nicoventures Trading Limited Article for use with apparatus for heating smokable material
US11672279B2 (en) 2011-09-06 2023-06-13 Nicoventures Trading Limited Heating smokeable material
US11825870B2 (en) 2015-10-30 2023-11-28 Nicoventures Trading Limited Article for use with apparatus for heating smokable material
US11924930B2 (en) 2015-08-31 2024-03-05 Nicoventures Trading Limited Article for use with apparatus for heating smokable material

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Cited By (14)

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Publication number Priority date Publication date Assignee Title
US6569907B1 (en) 1999-01-14 2003-05-27 Earth Chemical Co., Ltd. Heat transpiration preparation and method of the heat transpiration of chemical by using the same
WO2000042117A1 (en) * 1999-01-14 2000-07-20 Earth Chemical Co., Ltd. Heat transpiration preparation and method of the heat transpiration of chemical by using the same
US11672279B2 (en) 2011-09-06 2023-06-13 Nicoventures Trading Limited Heating smokeable material
US12041968B2 (en) 2011-09-06 2024-07-23 Nicoventures Trading Limited Heating smokeable material
US11241042B2 (en) 2012-09-25 2022-02-08 Nicoventures Trading Limited Heating smokeable material
US10036574B2 (en) 2013-06-28 2018-07-31 British American Tobacco (Investments) Limited Devices comprising a heat source material and activation chambers for the same
US10542777B2 (en) 2014-06-27 2020-01-28 British American Tobacco (Investments) Limited Apparatus for heating or cooling a material contained therein
US11659863B2 (en) 2015-08-31 2023-05-30 Nicoventures Trading Limited Article for use with apparatus for heating smokable material
US11924930B2 (en) 2015-08-31 2024-03-05 Nicoventures Trading Limited Article for use with apparatus for heating smokable material
US11064725B2 (en) 2015-08-31 2021-07-20 British American Tobacco (Investments) Limited Material for use with apparatus for heating smokable material
US11452313B2 (en) 2015-10-30 2022-09-27 Nicoventures Trading Limited Apparatus for heating smokable material
US11825870B2 (en) 2015-10-30 2023-11-28 Nicoventures Trading Limited Article for use with apparatus for heating smokable material
US12016393B2 (en) 2015-10-30 2024-06-25 Nicoventures Trading Limited Apparatus for heating smokable material
WO2022184946A1 (en) * 2021-03-02 2022-09-09 Global Termobiomasa S.L. Multipurpose autonomous thermal device

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