JP2007245040A - Granular material storing method and granular material storing device - Google Patents

Granular material storing method and granular material storing device Download PDF

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JP2007245040A
JP2007245040A JP2006073844A JP2006073844A JP2007245040A JP 2007245040 A JP2007245040 A JP 2007245040A JP 2006073844 A JP2006073844 A JP 2006073844A JP 2006073844 A JP2006073844 A JP 2006073844A JP 2007245040 A JP2007245040 A JP 2007245040A
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granular material
storage tank
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exothermic reaction
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JP4416747B2 (en
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Masaaki Takahashi
正章 高橋
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NGK Insulators Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a granular material storing method which stabilizes a granular material having exothermic property due to a low-temperature oxidation reaction or the like in an early time while storing it without causing thermorunaway and allows the granular material to be in a high-safety state enough to cause no ignition or fire without reducing a value as a fuel substitution, and also to provide a granular material storing device. <P>SOLUTION: Exothermic reaction of the granular material such as low-temperature oxidation reaction is promoted by supplying a gas such as an air to be an oxygen supply source to a storing container 1 for storing the granular material and heating it, and then the air supply is stopped to store the granular material. Preferably the air is supplied to the storing container 1 to stir the granular material. The granular material storing device has a function which prevents the thermorunaway of the granular material in the storing container 1 by cooling the granular material in the storing container 1. The exothermic reaction such as the low-temperature oxidation is controlled by controlling a gas supply amount into the storing container 1, a heating amount in the storing container, and a cooling amount based on temperature information in the storing container 1. The exothermic reaction such as the low-temperature oxidation is controlled by controlling temperature of the granular material within a range of 50-150°C. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、廃棄物を処理して得られる炭化物などの粉粒体を貯留しながら、熱暴走させることなく、安全な状態にするための粉粒体貯留方法および粉粒体貯留装置に関するものである。   TECHNICAL FIELD The present invention relates to a powder storage method and a powder storage device for making a safe state without causing thermal runaway while storing powder particles such as carbide obtained by processing waste. is there.

従来から、ごみ等の廃棄物を処理するにあたり、最終処分場(埋立地)の延命化を図るために、焼却やガス化溶融方法等により廃棄物の減量化が図られている。一方、最近では地球温暖化ガス(CO)の削減の要請から、ごみ等の廃棄物を焼却処理するのではなく、炭化炉で炭化処理して粉粒状の炭化物として回収し、有効利用を可能とする方法が提案されている。この炭化物は、例えば燃料としての石炭、コークス等の代替材や、金属の電気炉における溶湯表面の保温材等として利用できるため、更に省資源化に有効である。 Conventionally, when processing waste such as waste, in order to extend the life of the final disposal site (landfill), the amount of waste has been reduced by incineration, gasification and melting methods, and the like. On the other hand, recently, in response to a request for reduction of global warming gas (CO 2 ), waste such as waste is not incinerated, but carbonized in a carbonization furnace and recovered as granular carbide, enabling effective use A method has been proposed. This carbide can be used, for example, as an alternative material such as coal or coke as a fuel, or as a heat insulating material on the surface of a molten metal in a metal electric furnace, and thus is further effective for resource saving.

この粉粒状の炭化物は、遊離基・官能基等の反応性に富んだ基を多く含んでおり、低温酸化反応等により発熱する性質を持つ。従って、粉粒体の放熱量より発熱量の方が大きくなると、粉粒体が蓄熱し、この熱により粉粒体の低温酸化等の発熱反応がより促進され、ある一定の温度を超えると熱暴走して、最悪の場合発火し、火災に至る可能性がある。   This particulate carbide contains many reactive groups such as free radicals and functional groups, and has a property of generating heat due to a low-temperature oxidation reaction or the like. Therefore, when the calorific value is larger than the heat dissipation amount of the granular material, the granular material accumulates heat, and this heat further promotes an exothermic reaction such as low-temperature oxidation of the granular material, and heat exceeds when a certain temperature is exceeded. Runaway, in the worst case it could ignite and cause a fire.

炭化炉から回収された炭化物は、出荷するまで一旦サイロ等の貯留槽に貯留され(例えば3日間)、この貯留槽から貯留・運搬のため、小分けしてフレキシブルコンテナ等に収納される。貯留槽内で貯留される粉粒体は、フレキシブルコンテナ等に収納される時以外は貯留槽内を移動することがない。そのため、粉粒体が貯留槽内の一定の場所に留まって貯留され、蓄熱しやすくなる。粉粒体がある一定以上の温度に達した場合には、粉粒体は熱暴走し、最悪の場合発火・火災に至る可能性がある。粉粒体が発火して、燃焼状態になった場合には、貯留槽内部の酸素が不足し、CO(一酸化炭素)等の可燃性ガスが発生し、貯留槽が爆発する危険性がある。   The carbide recovered from the carbonization furnace is temporarily stored in a storage tank such as a silo until shipment (for example, for 3 days), and is stored in a flexible container or the like for storage and transportation from the storage tank. The granular material stored in the storage tank does not move in the storage tank except when stored in a flexible container or the like. Therefore, the granular material stays in a certain place in the storage tank and is stored, and heat is easily stored. When the granular material reaches a certain temperature or more, the granular material may run out of heat, and in the worst case, ignition or fire may occur. When the powder is ignited and becomes in a combustion state, there is a risk that oxygen in the storage tank will be insufficient, flammable gas such as CO (carbon monoxide) will be generated, and the storage tank will explode. .

上記問題を回避するために、貯留槽内部の温度上昇、又は可燃性ガスの検出により異常を検知した場合は、消火装置により、貯留槽内を不活性ガスの放出、水の散水等により消火するとともに、粉粒体を貯留槽から緊急排出するようにしているが、散水しながら排出された粉粒状の炭化物は、含水率が高くなり有姿発熱量(低位発熱量)が小さくなるため、燃料代替製品としての価値が著しく低下したものとなる。   In order to avoid the above problem, if an abnormality is detected by the temperature rise inside the storage tank or detection of flammable gas, the fire is extinguished by the release of inert gas, water sprinkling, etc. by the fire extinguishing device At the same time, the particulate matter is urgently discharged from the storage tank, but the particulate carbide discharged while sprinkling water increases the moisture content and reduces the solid calorific value (low calorific value). The value as a substitute product is significantly reduced.

一方で、上記問題を防止するために、貯留槽内部に流入する空気を遮断すると、粉粒体の低温酸化等の発熱反応が抑制され、更に粉粒体自身の重量により、粉粒体が貯留槽内で圧縮され、密な状態で貯留槽内に貯留されるので、低温酸化等の発熱反応が進行せず、フレキシブルコンテナ等に排出、収納する時に、粉粒体はまだ安定な状態となっていない。この結果、粉粒体を貯留槽からフレキシブルコンテナ等に小分けして収納するときに、粉粒体は空気と接触するため低温酸化等による発熱反応が起こり、最悪の場合には発火・火災に至るという問題があった。   On the other hand, if the air flowing into the storage tank is blocked in order to prevent the above problem, exothermic reactions such as low-temperature oxidation of the granular material are suppressed, and the granular material is stored by the weight of the granular material itself. Since it is compressed in the tank and stored in the storage tank in a dense state, exothermic reactions such as low-temperature oxidation do not proceed, and the powder particles are still stable when discharged and stored in a flexible container etc. Not. As a result, when the granular material is stored in small containers from a storage tank to a flexible container, the granular material comes into contact with air, so an exothermic reaction occurs due to low-temperature oxidation or the like, and in the worst case, ignition or fire occurs. There was a problem.

このため、フレキシブルコンテナ等で貯蔵、搬送中の粉粒体が、発火・火災を起こさないようにするために、初期の最も反応性に富む低温酸化等の発熱反応が進行し、比較的安定した状態になるまで、粉粒体をある程度の時間(例えば150時間)フレキシブルコンテナ等で貯蔵し、かつ貯蔵中は熱暴走しないように監視することが必要であった。従って、炭化物の貯留時において、貯留槽内で低温酸化が促進され、ある程度反応が落ち着いて安全性の高い炭化物として排出できる新たな貯留方法の開発が要望されていた。   For this reason, exothermic reactions such as low-temperature oxidation, which is the most reactive in the initial stage, have progressed relatively stably in order to prevent ignition of the powder and granular materials being stored and transported in flexible containers, etc. Until a state is reached, it is necessary to store the granular material in a flexible container or the like for a certain period of time (for example, 150 hours), and to monitor the storage so as not to cause thermal runaway during storage. Accordingly, there has been a demand for the development of a new storage method in which low-temperature oxidation is promoted in the storage tank and the reaction is settled to some extent and can be discharged as highly safe carbide during the storage of the carbide.

また、上記問題を解決するために、特許文献1に示すような炭化物生成施設が提案されている。この炭化物生成施設は、炭化物に脱酸素剤および脱酸素水溶液の少なくとも一方を供給し、脱気を行い袋内の酸素濃度を低減した状態で袋詰めをする施設である。しかしながら、この方法によって粉粒体の発熱を防止するには、大掛かりな設備が必要となり、また脱酸素剤や脱酸素水溶液が必要でありランニングコストが高くなるという問題がある。   Moreover, in order to solve the said problem, the carbide | carbonized_material production | generation facility as shown to patent document 1 is proposed. This carbide generation facility is a facility that supplies at least one of a deoxygenating agent and a deoxygenated aqueous solution to the carbide, performs degassing, and performs bagging in a state where the oxygen concentration in the bag is reduced. However, in order to prevent heat generation of the granular material by this method, there is a problem that large-scale equipment is required, and that a deoxygenating agent and a deoxygenated aqueous solution are necessary, resulting in high running costs.

特開2004−256122号公報Japanese Patent Laid-Open No. 2004-256122

本発明は上記のような問題点を解決して、低温酸化反応等による発熱性を有する粉粒体を、熱暴走させることなく、貯留しながら早期に安定化させ、燃料代替品としての価値を低下させないで、発火・火災を起こさないような安全性の高い状態となるようにするための粉粒体貯留方法および粉粒体貯留装置を提供することを目的として完成されたものである。   The present invention solves the above problems, stabilizes powder particles having exothermic properties due to low-temperature oxidation reaction, etc. at an early stage while storing them without thermal runaway, and has value as a fuel substitute. The present invention has been completed for the purpose of providing a granular material storage method and a granular material storage device for achieving a high safety state that does not cause ignition and fire without lowering.

上記課題を解決するためになされた本発明は、粉粒体を貯留する貯留槽内に空気等の酸素供給源を供給して、粉粒体の低温酸化等の発熱反応を促進させた後に、空気等の酸素供給源となり得る気体の供給を停止して貯留することを特徴とするものである。   The present invention made to solve the above problem is to supply an oxygen supply source such as air into a storage tank for storing the granular material, and promote an exothermic reaction such as low-temperature oxidation of the granular material, The supply of gas that can be an oxygen supply source such as air is stopped and stored.

なお、貯留槽内に供給する空気等気体により、粉粒体を撹拌して、粉粒体の低温酸化等の発熱反応を促進させることが好ましい。   In addition, it is preferable to stir the granular material with a gas such as air supplied into the storage tank to promote an exothermic reaction such as low-temperature oxidation of the granular material.

また、貯留槽内の粉粒体を加熱して、粉粒体の発熱反応を促進させることが好ましい。   Moreover, it is preferable to heat the exothermic reaction of a granular material by heating the granular material in a storage tank.

また、貯留槽内の粉粒体を冷却して、貯留槽内での熱暴走を防止しつつ、低温酸化等の発熱反応を促進させることが好ましい。   In addition, it is preferable to promote exothermic reaction such as low-temperature oxidation while cooling the granular material in the storage tank to prevent thermal runaway in the storage tank.

更に、貯留槽内の温度情報に基づき、貯留槽内への空気等の酸素供給源となり得る気体の供給量、貯留槽内の加熱量、貯留槽内の冷却量の1又は2以上を制御して、粉粒体の低温酸化等の発熱反応を制御することが好ましい。   Furthermore, based on the temperature information in the storage tank, one or more of the supply amount of gas that can be an oxygen supply source such as air into the storage tank, the heating amount in the storage tank, and the cooling amount in the storage tank are controlled. Thus, it is preferable to control an exothermic reaction such as low-temperature oxidation of the granular material.

なお、貯留槽内における粉粒体の温度を50〜150℃の範囲内に温度制御して、粉粒体の発熱反応を制御することが好ましい。   In addition, it is preferable to control the temperature of the granular material in the storage tank within a range of 50 to 150 ° C. to control the exothermic reaction of the granular material.

本発明の装置は、貯留槽の内部に空気を供給する空気等の気体供給装置を設けたことを特徴とすることが好ましい。   It is preferable that the apparatus of the present invention is provided with a gas supply device such as air for supplying air into the storage tank.

なお、貯留槽には、粉粒体を加熱する加熱装置及び粉粒体を冷却する冷却装置の少なくとも一方が設けられていることが好ましく、貯留槽内に設けられた温度センサーと、前記温度センサーで得られた温度情報に基づき、気体供給装置の気体供給量、加熱装置の加熱量、冷却装置の冷却量の1または2以上を制御する制御装置が設けられていることが好ましい。   The storage tank is preferably provided with at least one of a heating device for heating the powder and a cooling device for cooling the powder, and the temperature sensor provided in the storage tank and the temperature sensor It is preferable that a control device is provided for controlling one or more of the gas supply amount of the gas supply device, the heating amount of the heating device, and the cooling amount of the cooling device based on the temperature information obtained in (1).

なお、制御装置は、粉粒体の温度を50〜150℃の範囲内に温度制御することが好ましい。   In addition, it is preferable that a control apparatus temperature-controls the temperature of a granular material in the range of 50-150 degreeC.

本発明の粉粒体貯留方法および粉粒体貯留装置によれば、貯留槽内に空気等の気体を供給して粉粒体を撹拌することとしたので、粉粒体が貯留槽内一定の場所で留まり、蓄熱することによる発火・火災を防止し、また発火した場合の散水により、炭化物の燃料代替品としての価値を失うことを防止することができる。   According to the granular material storage method and the granular material storage device of the present invention, since the granular material is stirred by supplying gas such as air into the storage tank, the granular material is constant in the storage tank. It is possible to prevent ignition / fire due to staying at the place and storing heat, and to prevent loss of value as a fuel substitute for carbide by watering when ignited.

また、貯留槽内に空気等の酸素供給源となり得る気体を供給して、低温酸化等の発熱反応を促進させ、貯留しながら早期に安定化させることとすると、フレキシブルコンテナ等で炭化物が熱暴走しないように監視しながら長時間貯留する手間を省き、大掛かりな設備によらずに、ランニングコストが低く、粉粒体を安全性の高い状態にすることが可能となる。   In addition, if a gas that can serve as an oxygen supply source such as air is supplied into the storage tank to promote an exothermic reaction such as low-temperature oxidation and stabilize early while storing, the carbide will run away in a flexible container. Therefore, it is possible to save the labor of storing for a long time while monitoring so that the running cost is low and the granular material is in a high safety state without using large-scale equipment.

また、貯留槽内の粉粒体を加熱して、粉粒体の低温酸化等の発熱反応を促進させることとすると、効率よく粉粒体の低温酸化等の発熱反応を促進させて、粉粒体を早期に安全性の高い状態にすることが可能となる。   In addition, heating the granular material in the storage tank to promote exothermic reaction such as low-temperature oxidation of the granular material efficiently promotes exothermic reaction such as low-temperature oxidation of the granular material, The body can be brought into a highly safe state at an early stage.

貯留槽内の粉粒体を冷却して、低温酸化等の発熱反応を促進させることとすると、貯留槽内での熱暴走を防止しつつ、安全に粉粒体の低温酸化等の発熱反応を促進させることが可能となる。   If the granular material in the storage tank is cooled to promote an exothermic reaction such as low-temperature oxidation, an exothermic reaction such as low-temperature oxidation of the granular material can be safely performed while preventing thermal runaway in the storage tank. It becomes possible to promote.

更に、粉粒体の温度を測定する温度センサーと、この温度センサーで得られた温度情報に基づき、貯留槽内への気体供給量、粉粒体の加熱量、粉粒体の冷却量の1又は2以上を制御して、粉粒体の低温酸化を制御することとすると、粉粒体の熱暴走を防止しつつ、効率よく且つ安全に粉粒体の低温酸化等の発熱反応を促進させて、粉粒体を安全性の高い状態にすることが可能となる。   Furthermore, based on the temperature sensor that measures the temperature of the granular material and the temperature information obtained by this temperature sensor, 1 of the gas supply amount into the storage tank, the heating amount of the granular material, and the cooling amount of the granular material Or, if two or more are controlled to control the low temperature oxidation of the granular material, an exothermic reaction such as low temperature oxidation of the granular material is promoted efficiently and safely while preventing thermal runaway of the granular material. Thus, it becomes possible to make the powder and granule a highly safe state.

更に、粉粒体の温度を50〜150℃の範囲内に温度制御すると、粉粒体の熱暴走を防止しつつ、更に効率よく且つ安全に粉粒体の低温酸化等の発熱反応を促進させて、粉粒体を安全性の高い状態にすることが可能となる。   Furthermore, when the temperature of the granular material is controlled within the range of 50 to 150 ° C., it prevents thermal runaway of the granular material and promotes an exothermic reaction such as low-temperature oxidation of the granular material more efficiently and safely. Thus, it becomes possible to make the powder and granule a highly safe state.

本発明の粉粒体貯留方法により、粉粒体を比較的低温酸化等の発熱反応性に富んだ状態から、反応を促進させて安全性の高い状態とした場合には、粉粒体の可燃分及び有姿発熱量の低下率は実績によると3%以内となり、燃料代替製品等としての製品価値は低下しない。   When the granular material storage method according to the present invention promotes the reaction from a state of high exothermic reactivity such as relatively low-temperature oxidation to a highly safe state, the granular material is combustible. According to actual results, the rate of decrease in the amount of heat and solid heat generation is within 3%, and the product value as a fuel substitute product does not decrease.

以下に、図面を参照しつつ本発明の好ましい実施の形態を示す。
図1は本発明の実施の形態を示す貯留装置の説明図である。1はサイロ等の貯留槽であり、その内部に炭化炉から回収した粉粒体を、一旦(例えば3日)貯留するためのものである。この貯留槽1の形状は、例えば略円筒形や略直方体形であり、容量は例えば20〜30m3である。2は供給装置であり、炭化炉から回収された粉粒体を貯留槽1の内部に投入するものである。3はフレキシブルコンテナ4等に小分けして収納するための排出口であり、貯留槽1の底部に設けられている。
Hereinafter, preferred embodiments of the present invention will be described with reference to the drawings.
FIG. 1 is an explanatory view of a storage device showing an embodiment of the present invention. Reference numeral 1 denotes a storage tank such as a silo, which is used to temporarily store (for example, 3 days) the granular material collected from the carbonization furnace. The shape of the storage tank 1 is, for example, a substantially cylindrical shape or a substantially rectangular parallelepiped shape, and the capacity is, for example, 20 to 30 m 3 . Reference numeral 2 denotes a supply device for charging the granular material collected from the carbonization furnace into the storage tank 1. Reference numeral 3 denotes an outlet for subdividing and storing the flexible container 4 or the like, and is provided at the bottom of the storage tank 1.

粉粒体の低温酸化により、貯留槽1内の酸素が消費され、酸素濃度が低下すると、粉粒体の低温酸化等の発熱反応が阻害される。そこで、本発明の発明者は、貯留槽1の内部に新鮮な空気等の酸素供給源となり得る気体を供給して、粉粒体の低温酸化等の発熱反応を促進させるための気体供給装置5を設けることとした。   When the oxygen in the storage tank 1 is consumed by the low temperature oxidation of the powder and the oxygen concentration is lowered, exothermic reaction such as low temperature oxidation of the powder is inhibited. Therefore, the inventor of the present invention supplies a gas that can be an oxygen supply source such as fresh air into the storage tank 1 to promote an exothermic reaction such as low-temperature oxidation of the granular material 5. It was decided to provide.

この気体供給装置5は例えば図1のように貯留槽1の外部に設けられていてもよいし、貯留槽1の内部に設けられていてもよい。この気体供給装置5により、気体供給管6から貯留槽1の内部に空気等の気体が供給される。この気体供給管6は例えば、略円管や略角型管であり貯留槽1の内部に臨ませるように取り付けられている。この気体供給管6は図1に示すように、例えば貯留槽1内に突出した構造のものである。この気体供給管6の先端は閉じられていてもよいが、開放されていてもよい。   This gas supply device 5 may be provided outside the storage tank 1 as shown in FIG. 1, for example, or may be provided inside the storage tank 1. A gas such as air is supplied from the gas supply pipe 6 into the storage tank 1 by the gas supply device 5. The gas supply pipe 6 is, for example, a substantially circular pipe or a substantially square pipe, and is attached so as to face the inside of the storage tank 1. As shown in FIG. 1, the gas supply pipe 6 has a structure protruding into the storage tank 1, for example. The tip of the gas supply pipe 6 may be closed or may be opened.

この気体供給管6の外表面から気体供給管6内部に貫く孔が、気体供給管6に複数、形成され、この孔から気体供給管6内部の空気等の気体が貯留槽1に供給される。この気体供給管6は、金属、樹脂、陶製、セラミック等の多孔質の材質からなるものとして、気体供給管6の内部の空気等の気体を多孔から貯留槽1内に供給することとしてもよい。   A plurality of holes penetrating from the outer surface of the gas supply pipe 6 into the gas supply pipe 6 are formed in the gas supply pipe 6, and a gas such as air inside the gas supply pipe 6 is supplied to the storage tank 1 from the hole. . The gas supply pipe 6 may be made of a porous material such as metal, resin, porcelain, ceramic, etc., and gas such as air inside the gas supply pipe 6 may be supplied into the storage tank 1 from the porous. .

この気体供給管6は、貯留槽1を貫通するように取り付けられていてもよい。貯留槽1を貫通するように取り付けられた場合には、貯留槽1と貫通した先の気体供給管6を気体供給装置5に接続させて、気体供給管6内部の空気等の気体の一部が循環するような構造としてもよい。また、気体供給管6をU字型として気体供給管6内部の空気の一部が循環するような構造としてもよい。この気体供給管6は1本に限られず、2本以上の気体供給管6が貯留槽1に設けられていてもよい。この気体供給管6は、粉粒体の低温酸化等の発熱反応をより効果良く促進させるために、貯留槽1の底部付近に取り付けられていることが好ましい。   The gas supply pipe 6 may be attached so as to penetrate the storage tank 1. When it is attached so as to penetrate the storage tank 1, a part of the gas such as air inside the gas supply pipe 6 is connected by connecting the gas supply pipe 6 penetrating the storage tank 1 to the gas supply device 5. It is good also as a structure which circulates. The gas supply pipe 6 may be U-shaped so that a part of the air inside the gas supply pipe 6 circulates. The gas supply pipe 6 is not limited to one, and two or more gas supply pipes 6 may be provided in the storage tank 1. The gas supply pipe 6 is preferably attached in the vicinity of the bottom of the storage tank 1 in order to more effectively promote an exothermic reaction such as low-temperature oxidation of the granular material.

貯留槽1内の粉粒体の低温酸化等の発熱反応を促進させた後に、気体供給装置5を停止させて、貯留槽1内への空気等の供給を停止してもよいし、気体供給装置5を停止させなくても差し支えない。   After promoting an exothermic reaction such as low-temperature oxidation of the granular material in the storage tank 1, the gas supply device 5 may be stopped to stop the supply of air or the like into the storage tank 1, or the gas supply It does not matter if the device 5 is not stopped.

なお、気体供給装置5から貯留槽1内部に供給される空気等の気体は、粉粒体の低温酸化等の発熱反応を促進させるだけでなく、粉粒体の蓄熱部を空気等の気体が流通するので、この蓄熱部を冷却する効果もある。   The gas such as air supplied from the gas supply device 5 to the inside of the storage tank 1 not only promotes an exothermic reaction such as low-temperature oxidation of the granular material, but also the heat storage part of the granular material causes the gas such as air to flow. Since it circulates, there also exists an effect which cools this thermal storage part.

また、別の実施の形態として、気体供給管6の代わりに、図2に示すように、貯留槽1内部の上方に向けて開口しているノズル21が複数、気体供給管22に連結されている構造として、貯留槽1内部に空気等の気体を供給することとしてもよい。   As another embodiment, instead of the gas supply pipe 6, as shown in FIG. 2, a plurality of nozzles 21 opening upward in the storage tank 1 are connected to the gas supply pipe 22. It is good also as supplying gas, such as air, into the storage tank 1 inside as a structure.

また、別の実施の形態として、図3に示すように、貯留槽1の底部に気体供給板31を貯留槽1の底部に設けた構造として、貯留槽1内部に空気等を供給することとしてもよい。なお、この気体供給板31はこの板を貫く孔が複数、形成されていてもよいが、気体供給板21を金属、樹脂、陶製、セラミック等の多孔質の材質としてもよい。   As another embodiment, as shown in FIG. 3, as a structure in which a gas supply plate 31 is provided at the bottom of the storage tank 1, air or the like is supplied into the storage tank 1. Also good. The gas supply plate 31 may be formed with a plurality of holes penetrating the plate, but the gas supply plate 21 may be made of a porous material such as metal, resin, ceramic, ceramic, or the like.

粉粒体は、温度が上昇すると低温酸化等の発熱反応が促進される性質のものである。そこで、粉粒体を加熱して低温酸化等の発熱反応を促進させるために、貯留槽1には加熱装置13が設けられていることが好ましい。この加熱装置13は例えば、電熱線等により、熱を発生させて加熱してもよいが、貯留槽1自身に発熱する機能、例えばジャケット部に加熱媒体を流通させる等の機能を持たせ、粉粒体を貯留中に粉粒体を加熱させてもよいし、気体供給装置5に加熱装置13を設けて、貯留槽1内に温風を供給して粉粒体を加熱することとしてもよい。この加熱装置13により、貯留槽1内を、例えば50℃〜150℃に制御して、粉粒体の低温酸化等の発熱反応を促進させることが好ましい。   The granular material has a property that an exothermic reaction such as low-temperature oxidation is promoted when the temperature rises. Therefore, in order to heat the granular material and promote an exothermic reaction such as low-temperature oxidation, the storage tank 1 is preferably provided with a heating device 13. This heating device 13 may be heated by generating heat with, for example, a heating wire or the like. However, the heating device 13 has a function of generating heat in the storage tank 1 itself, for example, a function of circulating a heating medium in the jacket portion, and the like. The granular material may be heated while storing the granular material, or the heating device 13 may be provided in the gas supply device 5 to supply hot air into the storage tank 1 to heat the granular material. . It is preferable to promote the exothermic reaction such as low-temperature oxidation of the granular material by controlling the inside of the storage tank 1 to, for example, 50 ° C. to 150 ° C. with the heating device 13.

気体供給管6(22)、もしくは気体供給板31から空気等の気体を供給することにより、貯留槽1内の粉粒体が撹拌される。この粉粒体が撹拌されるので、均一に粉粒体の低温酸化等の発熱反応を促進させることが可能となる。しかも、粉粒体が貯留槽1内の一定の場所に留まることがなくなるので、蓄熱することなく、熱暴走による発火・火災を防止しつつ、粉粒体の低温酸化等の発熱反応を促進することが可能となる。なお、機械的な装置で粉粒体を撹拌しても差し支えない。   By supplying a gas such as air from the gas supply pipe 6 (22) or the gas supply plate 31, the granular material in the storage tank 1 is agitated. Since this granular material is agitated, it is possible to promote an exothermic reaction such as low-temperature oxidation of the granular material uniformly. In addition, since the granular material does not stay in a certain place in the storage tank 1, it promotes an exothermic reaction such as low-temperature oxidation of the granular material while preventing thermal ignition and fire without storing heat. It becomes possible. In addition, even if a granular material is stirred with a mechanical apparatus, it does not interfere.

しかし、粉粒体はある一定以上の温度になると、前述したように熱暴走し、発火・火災を起こしてしまう可能性がある。そこで、貯留槽1の内部の温度を制御するために、また粉粒体の熱暴走が発生しそうな緊急時に粉粒体を冷却するために、貯留槽1には冷却装置7が設けられていることが好ましい。貯留槽1内の温度が、例えば150℃を超えた場合、冷却装置7を作動させて貯留槽1内を冷却し、粉粒体の低温酸化反応を抑制して熱暴走を防止する。この冷却装置7は例えば、図1〜図3に示すように、貯留槽1内に冷却管8を設け、この冷却管8内に冷却媒体を送給し、この冷却管8の内部を流通する冷却媒体により、貯留槽1の内部を冷却して粉粒体を冷却するものである。冷却管8の内部を流通する冷却媒体は、例えば水であり、エチレングリコールやプロピレングリコール等の液体でもよく、空気等の気体であっても差し支えない。あるいは、気体供給装置5から供給される空気等の気体を冷却して粉粒体を冷却することとしてもよい。   However, when the temperature of the granular material reaches a certain level or more, as described above, there is a possibility that the thermal runaway may cause ignition and fire. Therefore, in order to control the temperature inside the storage tank 1 and to cool the granular material in an emergency in which thermal runaway of the granular material is likely to occur, the storage tank 1 is provided with a cooling device 7. It is preferable. When the temperature in the storage tank 1 exceeds, for example, 150 ° C., the cooling device 7 is operated to cool the storage tank 1, and the low temperature oxidation reaction of the granular material is suppressed to prevent thermal runaway. For example, as shown in FIGS. 1 to 3, the cooling device 7 is provided with a cooling pipe 8 in the storage tank 1, a cooling medium is fed into the cooling pipe 8, and the inside of the cooling pipe 8 is circulated. The inside of the storage tank 1 is cooled by the cooling medium to cool the granular material. The cooling medium flowing through the inside of the cooling pipe 8 is, for example, water, may be a liquid such as ethylene glycol or propylene glycol, or may be a gas such as air. Or it is good also as cooling gas, such as air supplied from the gas supply apparatus 5, and cooling a granular material.

粉粒体の低温酸化等の発熱反応を促進させ、また粉粒体が貯留槽1内で熱暴走することなく、且つ効率よく粉粒体の低温酸化等の発熱反応を促進させるために、貯留槽1内部の気体供給量、加熱量もしくは冷却量を制御することが好ましい。そこで、例えば貯留槽1内の中心付近に貯留槽中心部温度センサー9、貯留槽1の底部に貯留槽底部温度センサー10、貯留槽1の上部に貯留槽上部温度センサー11を設け、これらの温度センサーから測定される温度情報に基づいて、気体供給装置5の気体供給量、加熱装置13の加熱量、冷却装置7の冷却量を制御する制御装置12が設けられていることが好ましい。   In order to promote exothermic reaction such as low-temperature oxidation of the granular material, and to promote exothermic reaction such as low-temperature oxidation of the granular material efficiently without causing thermal runaway in the storage tank 1 It is preferable to control the gas supply amount, heating amount or cooling amount inside the tank 1. Therefore, for example, a storage tank center temperature sensor 9 is provided near the center of the storage tank 1, a storage tank bottom temperature sensor 10 is provided at the bottom of the storage tank 1, and a storage tank upper temperature sensor 11 is provided above the storage tank 1, and these temperatures are provided. It is preferable to provide a control device 12 that controls the gas supply amount of the gas supply device 5, the heating amount of the heating device 13, and the cooling amount of the cooling device 7 based on temperature information measured from the sensor.

貯留槽中心部温度センサー9、貯留槽底部温度センサー10、貯留槽上部温度センサー11のそれそれで測定された温度が、それぞれ規定の閾値(例えば150℃)を超えた場合、もしくはこれらの温度情報の組み合わせにより異常と判断された場合には、貯留槽1内の粉粒体が熱暴走する危険があると制御装置12が判断する。   When the temperature measured by each of the storage tank center temperature sensor 9, the storage tank bottom temperature sensor 10, and the storage tank upper temperature sensor 11 exceeds a specified threshold value (for example, 150 ° C.), or When it is determined that the abnormality is caused by the combination, the control device 12 determines that there is a risk that the granular material in the storage tank 1 is thermally runaway.

前記判断に基づき、制御装置12は気体供給装置5を制御して、貯留槽1内に供給される空気の量を通常量よりも少なくするか、もしくは貯留槽1内への空気の供給を遮断して、粉粒体の低温酸化等の発熱反応を抑制する。   Based on the determination, the control device 12 controls the gas supply device 5 so that the amount of air supplied into the storage tank 1 is less than the normal amount, or the supply of air into the storage tank 1 is shut off. Thus, an exothermic reaction such as low-temperature oxidation of the granular material is suppressed.

また、前記判断に基づき、制御装置12は加熱装置13を制御し、加熱装置13による粉粒体の加熱量を通常時より弱めるか、もしくは粉粒体の加熱を停止させて、粉粒体の低温酸化等の発熱反応が促進されることを防止する。   Further, based on the above determination, the control device 12 controls the heating device 13 to weaken the heating amount of the granular material by the heating device 13 than usual, or to stop the heating of the granular material, Prevents exothermic reactions such as low-temperature oxidation from being promoted.

また、前記判断に基づき、制御装置12は冷却装置7を作動させて、粉粒体を冷却し、粉粒体の低温酸化等の発熱反応を抑制させる。   Further, based on the determination, the control device 12 operates the cooling device 7 to cool the granular material and suppress exothermic reactions such as low-temperature oxidation of the granular material.

また、この制御装置12は前述したように粉粒体の熱暴走を防止するだけでなく、気体供給装置5による貯留槽1内への気体供給量、加熱装置13による加熱量、冷却装置7による冷却量を制御して、貯留槽1内の温度を例えば50〜150℃の範囲内に温度制御することにより、粉粒体の低温酸化等の発熱反応を制御し、粉粒体を効率よく安全性の高い状態にすることが可能となる。   Further, as described above, the control device 12 not only prevents thermal runaway of the granular material, but also supplies the gas supplied into the storage tank 1 by the gas supply device 5, the heating amount by the heating device 13, and the cooling device 7. By controlling the amount of cooling and controlling the temperature in the storage tank 1 within a range of 50 to 150 ° C., for example, the exothermic reaction such as low-temperature oxidation of the powder is controlled, and the powder is efficiently and safely It becomes possible to make a state with high property.

以上に説明したように、本発明によれば大規模な装置を用いることなく、低温酸化反応等による発熱性を有する粉粒体を早期に安定化させ、確実に粉粒体の熱暴走による発火・火災を防止することができる。   As described above, according to the present invention, without using a large-scale apparatus, the granular material having exothermic properties due to a low-temperature oxidation reaction or the like is stabilized at an early stage, and ignition by thermal runaway of the granular material is surely performed.・ Fire can be prevented.

なお、本発明の粉粒体貯留槽は、廃棄物を炭化炉で処理した際に生成される炭化物の保管貯留だけでなく、RDF(ゴミ固形化燃料)や金属切削屑等、貯留中に熱暴走し、発火する危険がある物質の貯留方法にも用いることができるのはいうまでもない。   In addition, the granular material storage tank of the present invention not only stores and stores carbides generated when wastes are processed in a carbonization furnace, but also heats RDF (dust solidified fuel), metal cutting waste, and the like during storage. Needless to say, it can also be used to store materials that are at risk of running away and catching fire.

以上、現時点において、もっとも、実践的であり、かつ好ましいと思われる実施形態に関連して本発明を説明したが、本発明は、本願明細書中に開示された実施形態に限定されるものではなく、請求の範囲および明細書全体から読み取れる発明の要旨あるいは思想に反しない範囲で適宜変更可能であり、そのような変更を伴う粉粒体貯留方法および粉粒体貯留装置もまた技術的範囲に包含されるものとして理解されなければならない。   Although the present invention has been described above in connection with the most practical and preferred embodiments at the present time, the present invention is not limited to the embodiments disclosed herein. The powder storage method and the powder storage device with such changes are also within the technical scope without departing from the spirit or idea of the invention that can be read from the claims and the entire specification. It must be understood as included.

本発明の実施の形態を示す説明図である。It is explanatory drawing which shows embodiment of this invention. 本発明の実施の形態を示す説明図である。It is explanatory drawing which shows embodiment of this invention. 本発明の実施の形態を示す説明図である。It is explanatory drawing which shows embodiment of this invention.

符号の説明Explanation of symbols

1 貯留槽
2 供給装置
3 排出口
4 フレキシブルコンテナ
5 気体供給装置
6 気体供給管
7 冷却装置
8 冷却管
9 貯留槽内温度センサー
10 貯留槽底部温度センサー
11 貯留槽上部温度センサー
12 制御装置
13 加熱装置
21 ノズル
22 気体供給管
31 気体供給板
DESCRIPTION OF SYMBOLS 1 Storage tank 2 Supply apparatus 3 Outlet 4 Flexible container 5 Gas supply apparatus 6 Gas supply pipe 7 Cooling apparatus 8 Cooling pipe 9 Reservoir temperature sensor 10 Reservoir bottom temperature sensor 11 Reservoir upper temperature sensor 12 Control apparatus 13 Heating apparatus 21 Nozzle 22 Gas supply pipe 31 Gas supply plate

Claims (13)

貯留槽内に貯留された、発熱性を有する粉粒体を貯留する貯留槽内に酸素供給源となり得る気体を供給して、粉粒体の発熱反応を促進させた後に、酸素供給源となり得る気体の供給を停止して貯留することを特徴とする粉粒体貯留方法。   A gas that can be an oxygen supply source is supplied into a storage tank that stores exothermic granular material stored in the storage tank, and can be an oxygen supply source after promoting an exothermic reaction of the granular material. A granular material storage method, wherein gas supply is stopped and stored. 貯留槽内に供給する気体により、粉粒体を撹拌して、粉粒体の発熱反応を促進させることを特徴とする請求項1に記載の粉粒体貯留方法。   The granular material storage method according to claim 1, wherein the granular material is stirred by a gas supplied into the storage tank to promote an exothermic reaction of the granular material. 貯留槽内の粉粒体を加熱して、粉粒体の発熱反応を促進させることを特徴とする請求項1又は2のいずれかに記載の粉粒体貯留方法。   The granular material storage method according to claim 1, wherein the granular material in the storage tank is heated to promote an exothermic reaction of the granular material. 貯留槽内の粉粒体を冷却して、貯留槽内での熱暴走を防止しつつ、発熱反応を促進させることを特徴とする請求項1乃至3のいずれかに記載の粉粒体貯留方法。   The granular material storage method according to any one of claims 1 to 3, wherein the granular material in the storage tank is cooled to prevent thermal runaway in the storage tank and promote an exothermic reaction. . 貯留槽内の温度情報に基づき、貯留槽内へ酸素供給源となり得る気体の供給量、貯留槽内の加熱量、貯留槽内の冷却量の1又は2以上を制御して、粉粒体の発熱反応を制御することを特徴とする請求項1乃至4のいずれかに記載の粉粒体貯留方法。   Based on the temperature information in the storage tank, one or more of the supply amount of gas that can be an oxygen supply source into the storage tank, the heating amount in the storage tank, and the cooling amount in the storage tank are controlled, and An exothermic reaction is controlled, The granular material storage method in any one of Claims 1 thru | or 4 characterized by the above-mentioned. 貯留槽内における粉粒体の温度を50〜150℃の範囲内に温度制御して、粉粒体の発熱反応を促進させることを特徴とする請求項1乃至5のいずれかに記載の粉粒体貯留方法。   The temperature of the granular material in a storage tank is temperature-controlled within the range of 50-150 degreeC, and the exothermic reaction of a granular material is accelerated | stimulated, The granular material in any one of Claim 1 thru | or 5 characterized by the above-mentioned. Body storage method. 発熱反応は、低温酸化反応であることを特徴とする請求項1乃至6のいずれかに記載の粉粒体貯留方法。   The granular material storage method according to claim 1, wherein the exothermic reaction is a low-temperature oxidation reaction. 酸素供給源となり得る気体は、空気であることを特徴とする請求項1乃至7のいずれかに記載の粉粒体貯留方法。   The method for storing granular materials according to claim 1, wherein the gas that can serve as an oxygen supply source is air. 発熱性を有する粉粒体を貯留する粉粒体貯留装置において、貯留槽の内部に気体を供給する気体供給装置を設けたことを特徴とする粉粒体貯留装置。   In the granular material storage apparatus which stores the granular material which has exothermic property, the gas supply apparatus which supplies gas into the inside of a storage tank was provided, The granular material storage apparatus characterized by the above-mentioned. 貯留槽には、貯留槽内の粉粒体を加熱する加熱装置及び、貯留槽内の粉粒体を冷却する冷却装置の少なくとも一方が設けられていることを特徴とする請求項9に記載の粉粒体貯留装置。   The storage tank is provided with at least one of a heating device for heating the granular material in the storage tank and a cooling device for cooling the granular material in the storage tank. Powder storage device. 貯留槽内に設けられた温度センサーと、前記温度センサーで得られた温度情報に基づき、気体供給装置の気体の供給量、加熱装置の加熱量、冷却装置の冷却量の1又は2以上を制御する制御装置が設けられていることを特徴とする請求項9又は10のいずれかに記載の粉粒体貯留装置。   Based on the temperature sensor provided in the storage tank and the temperature information obtained by the temperature sensor, one or more of the gas supply amount of the gas supply device, the heating amount of the heating device, and the cooling amount of the cooling device are controlled. The control apparatus which performs is provided, The granular material storage apparatus in any one of Claim 9 or 10 characterized by the above-mentioned. 制御装置は、貯留槽内の粉粒体の温度を50〜150℃の範囲内に温度制御することを特徴とする請求項11に記載の粉粒体貯留装置。   The control apparatus controls the temperature of the granular material in the storage tank within a range of 50 to 150 ° C, and the granular storage apparatus according to claim 11. 貯留槽の内部に供給する気体は、空気であることを特徴とする請求項9乃至12のいずれかに記載の粉粒体貯留装置。   The powder storage device according to any one of claims 9 to 12, wherein the gas supplied to the inside of the storage tank is air.
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CN104249871A (en) * 2014-09-04 2014-12-31 浙江华腾牧业有限公司 Molasses heat-insulating storage tank and molasses storage method thereof
CN105035573A (en) * 2015-07-15 2015-11-11 湖州荣德粮油有限公司 Oil storage tank with heat exchange function
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JP2013082892A (en) * 2011-09-30 2013-05-09 Metawater Co Ltd Manufacturing method and manufacturing system of carbonized material
KR101430590B1 (en) * 2012-03-21 2014-08-18 주식회사 드웰 Cooling system for watertank
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CN105035573A (en) * 2015-07-15 2015-11-11 湖州荣德粮油有限公司 Oil storage tank with heat exchange function
CN112239029A (en) * 2020-11-18 2021-01-19 江苏美梵生物科技有限公司 Bio-based material is with equipment of storing of thermostatic control of being convenient for
CN112239029B (en) * 2020-11-18 2021-12-31 江苏美梵生物科技有限公司 Bio-based material is with equipment of storing of thermostatic control of being convenient for

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