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JP4404572B2 - Separation and collection method of unused recovered powder - Google Patents
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JP4404572B2 - Separation and collection method of unused recovered powder - Google Patents

Separation and collection method of unused recovered powder Download PDF

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Publication number
JP4404572B2
JP4404572B2 JP2003129195A JP2003129195A JP4404572B2 JP 4404572 B2 JP4404572 B2 JP 4404572B2 JP 2003129195 A JP2003129195 A JP 2003129195A JP 2003129195 A JP2003129195 A JP 2003129195A JP 4404572 B2 JP4404572 B2 JP 4404572B2
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Japan
Prior art keywords
sieve
unused
recovered powder
extinguishing agent
powder
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JP2003129195A
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JP2004329551A (en
Inventor
泰欣 福田
祥典 奥川
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Yamato Protec Corp
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Yamato Protec Corp
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/70Chemical treatment, e.g. pH adjustment or oxidation

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  • Health & Medical Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Processing Of Solid Wastes (AREA)
  • Combined Means For Separation Of Solids (AREA)
  • Fire-Extinguishing Compositions (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、消火器から抜き出した未使用回収粉末消火薬剤を再利用原料として使用するのに好適な未使用回収粉末消火薬剤の分離回収方法に関する。
【0002】
【従来の技術】
現在市販されている粉末消火薬剤はそのほとんどがリン酸アンモニウム及び硫酸アンモニウムを主成分としており、その他の市販されている粉末消火薬剤として重炭酸金属塩類(具体的には重炭酸ナトリウム)を主成分とするものがあり、前者がABC粉末、後者がBC粉末と通称されている。また、ABC粉末を用いている消火器(ABC粉末消火器)やBC粉末を用いている消火器(BC粉末消火器)に対しては、定期的な点検や粉末消火薬剤の詰め替え作業、老朽化した消火器の回収作業などが行われ、その際に上記の各消火器から取り出した未使用の回収粉末消火薬剤が生じる。そこで、こうして発生した未使用回収粉末消火薬剤を一旦回収し、回収した未使用粉末消火薬剤を再利用原料として使用することが考えられている。
【0003】
前記ABC粉末やBC粉末といった粉末消火薬剤の回収形態として、消火薬剤が充填されたままの消火器が処理施設に搬入される場合と、消火器に充填されている粉末消火薬剤をユーザ、回収業者または営業担当者などが現地で1斗缶などの受入容器に移し、その受入容器を処理施設に搬入して回収する場合がある(特願2002−074858。)。
【0004】
【発明が解決しようとする課題】
ところが、消火器に充填されている未使用粉末消火薬剤をユーザ、回収業者または営業担当者などが現地で1斗缶などの受入容器に移し、その受入容器を処理施設に搬入して回収する回収形態では、1斗缶などの受入容器に消火器の部品、工場廃材、ゴミなどの異物が投入されて未使用粉末消火薬剤に混入した状態で処理施設に搬入される場合が起こり得る。このように、1斗缶などの受入容器の内部で前記の異物が未使用粉末消火薬剤に隠れた状態で混入していると、目視によって異物を確認して除去する作業が非常に煩雑であるばかりか、異物を確実に除去することが困難である問題点を有している。
【0005】
本発明は、このような事情を考慮してなされたもので、1斗缶などの受入容器に移された未使用回収粉末消火薬剤に混入している異物を該未使用回収粉末消火薬剤から簡単かつ確実に分離して、未使用粉末消火薬剤を再利用原料として使用できるようにする未使用粉末消火薬剤の分離回収方法を提供することを目的としている。
【0006】
【課題を解決するための手段】
前記目的を達成するために、請求項1に記載の発明は、消火器から抜き出した未使用回収粉末消火薬剤を受入容器に移し、この未使用回収粉末消火薬剤を、1段目の篩(以下、フルイという)から最終段のフルイにかけて網目数が増加する複数段のフルイを備えたフルイ分離装置に投入してフルイ分離処理を施し、最終段のフルイを通過することでフルイ分離処理された未使用回収粉末消火薬剤から磁気吸着装置により磁性金属を吸着除去することを特徴としている。
【0007】
また、請求項2に記載の発明のように、前記1段目のフルイの目開きを1〜5cmに設定し、最終段のフルイの網目数を83メッシュに設定することが好ましい。
【0008】
【0009】
請求項1に記載の発明によれば、1斗缶などの受入容器に移された未使用回収粉末消火薬剤に混入している異物は、フルイ分離装置によって確実に捕捉して、未使用回収粉末消火薬剤から分離除去することができる。さらに、異物である磁性金属粉が未使用粉末消火薬剤に同伴して回収される不都合を確実に防止することができる。
【0010】
請求項2に記載の発明によれば、1段目のフルイによって、消火器の部品、工場廃材などの大きい異物を捕捉して未使用回収粉末消火薬剤から分離除去することができる。また、最終段のフルイによって、83メッシュを超える粒径のゴミなどの微細な異物を捕捉して未使用回収粉末消火薬剤から分離除去することができるとともに、粒径が基準粒径(83メッシュ)以下で再利用原料として使用可能な未使用粉末消火薬剤のみを回収することができる。
【0011】
【0012】
【発明の実施の形態】
以下、本発明の一実施の形態を図面に基づいて説明する。図1は、本発明の一実施の形態に適用されるフローチャートである。この図において、1本の消火器には、平均約3Kgの未使用回収粉末消火薬剤が充填されており、5本の消火器から抜き出した約15Kgの未使用回収粉末消火薬剤がユーザ、回収業者または営業担当者などによって、現地で1斗缶などの受入容器に移されている。前記5本の消火器から抜き出した約15Kgの未使用回収粉末消火薬剤が移されている1斗缶などの受入容器の複数個が処理施設1に搬入される。
【0013】
前記処理施設1には、フルイ分離装置2が設置されている。フルイ分離装置2は、1段目のフルイ2Aから最終段のフルイ2Cにかけて網目数が増加する3段のフルイ2A,2B,2Cを備えており、1段目のフルイ2Aは、その目開きが1〜5cmに設定され、最終段のフルイ2Cの網目数は83メッシュに設定されている。また、2段目のフルイ2Bの網目数は50メッシュ程度であればよい。なお、1〜3段目のフルイ2A〜2Cは、図示されていない電磁式または電動式などの周知のフルイ原動機によって駆動される。
【0014】
処理施設1に搬入された複数個の1斗缶などの受入容器に移されている未使用回収粉末消火薬剤は、前記フルイ原動機によって駆動されているフルイ分離装置2における1段目のフルイ2Aに順次投入される。1段目のフルイ2Aに投入された未使用回収粉末消火薬剤には、消火器の部品、磁性金属を含む工場廃材、ゴミなどの異物が混入している。これらの異物における消火器の部品、磁性金属を含む工場廃材などの大型の異物は、1段目のフルイ2Aによって捕捉して未使用回収粉末消火薬剤から分離除去することができる。
【0015】
1段目のフルイ2Aを通過した未使用回収粉末消火薬剤は、2段目のフルイ2Bに送られる。2段目のフルイ2Bに送られた未使用回収粉末消火薬剤には、前記1段目のフルイ2Aによって捕捉されて分離除去された大型の異物よりも小さく、未使用回収粉末消火薬剤の粒径よりも十分に大きい磁性金属を含む工場廃材やゴミなどの中型の異物が混入している。これら中型の異物は、2段目のフルイ2Bによって捕捉して未使用回収粉末消火薬剤から分離除去することができる。
【0016】
1段目のフルイ2Aによって異物における大型の消火器の部品、磁性金属を含む工場廃材などの異物が分離除去されていることにより、2段目のフルイ2Bに負荷される重力が大幅に軽減されるので、2段目のフルイ2Bが50メッシュ程度の網目数を有する線径が細い構造であっても、中型の異物による線ののびや網目の損傷などを回避して適正なフルイを実行することができる。
【0017】
2段目のフルイ2Bを通過した未使用回収粉末消火薬剤は、3段目のフルイ2Cに送られる。3段目のフルイ2Cに送られた未使用回収粉末消火薬剤には、前記2段目のフルイ2Bによって捕捉されて分離除去された中型の異物よりも小さく、しかも未使用回収粉末消火薬剤の粒径よりも若干大きい磁性金属を含む工場廃材やゴミなどの微細な異物が混入している。これら微細な異物は、3段目のフルイ2Cによって捕捉して未使用回収粉末消火薬剤から分離除去することができる。すなわち、83メッシュを超える粒径の磁性金属を含む工場廃材やゴミなどの微細な異物を捕捉して未使用回収粉末消火薬剤から分離除去することができる。
【0018】
2段目のフルイ2Bによって異物における中型の消火器の部品、工場廃材などの異物が分離除去されていることにより、3段目のフルイ2Cに負荷される重力がさらに軽減されるので、3段目のフルイ2Cが83メッシュの網目数を有する線径が極細の構造であっても、微細な異物による線ののびや網目の損傷などを回避して適正なフルイを実行することができる。
【0019】
3段目のフルイ2Cを通過した未使用回収粉末消火薬剤は、その粒径が国家検定規格で定められた基準粒径(83メッシュ)以下である。この3段目のフルイ2Cを通過した未使用回収粉末消火薬剤は、永久磁石または電磁石を備えた磁気吸着装置3に送られ、ここでは、未使用回収粉末消火薬剤とともに3段目のフルイ2Cを通過した磁性金属(磁性金属粉)が吸着除去される。
【0020】
磁気吸着装置3を通過することで磁性金属粉が吸着除去された未使用回収粉末消火薬剤は、バッチタンク4に100Kgずつ投入してバッチ化され、バッチ化された未使用回収粉末消火薬剤からサンプルを抽出して、気泡発生の有無を調べる気泡試験、圧力上昇を調べる圧力試験、ガス発生の有無を調べるガス分析、色彩計による色彩試験、pH計によるpH試験などを行って、異種の未使用回収粉末消火薬剤(BC粉末)や土などの異物の混入を認めた場合には、前記バッチ化した100Kg相当の未使用回収粉末消火薬剤を投棄し、異種の未使用回収粉末消火薬剤(BC粉末)や土などの異物の混入が認められない場合には、分級ロータなどの分離装置5によりシリコンコーティングされたホワイトカーボンを分離除去して、リン酸アンモニウム及び硫酸アンモニウムを主成分とした未使用回収粉末消火薬剤をバッチタンク6に投入し、投入された未使用回収粉末消火薬剤からサンプルを抽出して、X線回折分析装置によりリン酸アンモニウムと硫酸アンモニウムの割合を測定して、天秤計量装置7により計量された500Kgの未使用回収粉末消火薬剤を1つのコンテナパックに収容し、コンテナパックに収容した未使用回収粉末消火薬剤を再利用原料として使用することができる。なお、X線回折分析装置により測定されたリン酸アンモニウムと硫酸アンモニウムの割合は、未使用回収粉末消火薬剤を再利用原料として使用する場合に補充される新しいリン酸アンモニウムと硫酸アンモニウムの補充量の目安になる。
【0021】
なお、前記実施の形態では、1段目のフルイ2Aと最終段のフルイ2Cの間に、1つのフルイ2Bを配置した3段のフルイ2A,2B,2Cを備えたフルイ分離装置2によってフルイをかける方式で説明しているが、1段目のフルイ2Aと最終段のフルイ2Cの間に複数のフルイを配置した4段以上のフルイを備えているフルイ分離装置2によってフルイをかける方式であってもよい。
【0022】
【発明の効果】
以上のように、本発明に係る未使用回収粉末消火薬剤の分離回収方法は構成されているので、以下のような格別の効果を奏する。
【0023】
請求項1に記載の発明によれば、1斗缶などの受入容器に移された未使用粉末消火薬剤に混入している異物を未使用粉末消火薬剤から簡単に分離して、未使用粉末消火薬剤のみを確実に回収して再利用原料として使用することができる。さらに、未使用回収粉末消火薬剤とともに最終段のフルイを通過した磁性金属(磁性金属粉)を吸着除去して、再利用原料として使用可能な未使用粉末消火薬剤の純度低下を回避することができる。
【0024】
請求項2に記載の発明によれば、その粒径が基準粒径(83メッシュ)以下の再利用原料として使用可能な未使用粉末消火薬剤を回収することができるばかりか、未使用回収粉末消火薬剤に混入している大型の異物から微細な異物にかけて、段階的に分離除去されることにより、後段のフルイに負荷される重力を軽減して、異物による線ののびや網目の損傷などを回避して、適正なフルイの実行に寄与することができる。
【0025】
【図面の簡単な説明】
【図1】 本発明の一実施の形態に適用されるフローチャートである。
【符号の説明】
2 フルイ分離装置
2A 1段目のフルイ
2C 3段目のフルイ(最終段のフルイ)
3 磁気吸着装置
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for separating and recovering an unused recovered powder fire extinguisher that is suitable for using an unused recovered powder extinguisher extracted from a fire extinguisher as a reuse material.
[0002]
[Prior art]
Most commercially available powder fire extinguishing agents are mainly composed of ammonium phosphate and ammonium sulfate, and other commercially available powder fire extinguishing agents are based on metal bicarbonates (specifically sodium bicarbonate). The former is commonly called ABC powder and the latter is commonly called BC powder. In addition, for fire extinguishers that use ABC powder (ABC powder fire extinguishers) and fire extinguishers that use BC powder (BC powder fire extinguishers), regular inspections, refilling of powder fire extinguishing agents, aging The fire extinguisher is collected, and at that time, unused recovered powder fire extinguishing chemicals are taken out from the respective fire extinguishers. Therefore, it is considered that the unused recovered powder extinguisher generated in this way is once recovered and the recovered unused powder extinguisher is used as a reuse material.
[0003]
As a recovery form of the powder extinguisher such as ABC powder or BC powder, when a fire extinguisher filled with the fire extinguishing agent is brought into a processing facility, the powder extinguishing agent filled in the fire extinguisher is collected by a user or a collector. Alternatively, there may be a case where a sales representative or the like moves to a receiving container such as a dough can at the site and carries the receiving container into a processing facility for collection (Japanese Patent Application No. 2002-074858).
[0004]
[Problems to be solved by the invention]
However, the unused powder extinguishing agent filled in the fire extinguisher is collected by the user, collection company or sales representative, etc. at the site, moving it to a receiving container such as a dough can, and bringing the receiving container into a processing facility for recovery. In the embodiment, there may be a case where foreign materials such as fire extinguisher parts, factory waste materials, and dust are put into a receiving container such as a single funnel and are carried into a processing facility in a state of being mixed in an unused powder fire extinguishing agent. Thus, when the foreign matter is mixed in an unused powder fire-extinguishing agent in a receiving container such as a one-dot can, it is very complicated to visually confirm and remove the foreign matter. In addition, there is a problem that it is difficult to reliably remove foreign matters.
[0005]
The present invention has been made in view of such circumstances, and foreign substances mixed in an unused recovered powder fire extinguisher transferred to a receiving container such as a 1-to-can can be easily removed from the unused recovered powder fire extinguisher. Another object of the present invention is to provide a method for separating and recovering an unused powder fire extinguishing agent that can be reliably separated and used as a raw material for reuse.
[0006]
[Means for Solving the Problems]
In order to achieve the object, the invention according to claim 1 transfers the unused recovered powder fire extinguishing agent extracted from the fire extinguisher to a receiving container, and the unused recovered powder extinguishing agent is passed through a first-stage sieve (hereinafter referred to as a first-stage sieve). , and facilities the sieve separation process was put into sieve separation apparatus having a plurality of stages of sieve mesh number increases sieved in the final stage from) that sieve were sieve separation process by passing through a sieve of the last stage It is characterized in that magnetic metal is adsorbed and removed from unused recovered powder fire extinguishing agent by a magnetic adsorption device .
[0007]
Further, as in the invention described in claim 2, it is preferable that the opening of the first stage sieve is set to 1 to 5 cm, and the number of meshes of the final stage sieve is set to 83 mesh.
[0008]
[0009]
According to the first aspect of the present invention, the foreign matter mixed in the unused recovered powder fire extinguisher transferred to a receiving container such as a 1-can can is reliably captured by the sieve separator and used recovered powder. Can be separated and removed from fire extinguishing agents. Furthermore, it is possible to reliably prevent inconvenience that the magnetic metal powder, which is a foreign substance, is collected with the unused powder fire extinguishing agent.
[0010]
According to the second aspect of the present invention, large foreign matters such as fire extinguisher parts and factory waste can be captured and separated from unused recovered powder fire extinguishing chemicals by the first stage sieve. In addition, fine particles such as dust having a particle size exceeding 83 mesh can be captured and separated from unused recovered powder fire extinguishing agent by the final stage sieve, and the particle size can be the reference particle size (83 mesh). Only unused powder fire extinguishing agents that can be used as reusable raw materials can be recovered below.
[0011]
[0012]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, an embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a flowchart applied to an embodiment of the present invention. In this figure, one fire extinguisher is filled with an average of about 3 Kg of unused recovered powder fire extinguishing agent, and about 15 Kg of unused recovered powder extinguishing agent extracted from five fire extinguishers is used by the user and the recovery contractor. Or it has been moved locally to a receiving container such as a 1 can by a sales representative. A plurality of receiving containers, such as a 1-can, to which about 15 kg of unused recovered powder fire extinguishing agent extracted from the five fire extinguishers has been transferred are carried into the processing facility 1.
[0013]
The processing facility 1 is provided with a sieve separator 2. The sieve separator 2 is provided with three-stage sieves 2A, 2B, and 2C in which the number of meshes increases from the first-stage sieve 2A to the final-stage sieve 2C. The first-stage sieve 2A has a mesh opening. It is set to 1 to 5 cm, and the number of meshes of the final stage 2C is set to 83 mesh. The number of meshes of the second stage sieve 2B may be about 50 mesh. The first to third stage sieves 2A to 2C are driven by a well-known sieve motor such as an electromagnetic type or an electric type (not shown).
[0014]
The unused recovered powder extinguishing agent transferred to a receiving container such as a plurality of one-cans carried into the processing facility 1 is transferred to the first stage sieve 2A in the sieve separator 2 driven by the sieve motor. It is thrown sequentially. The unused recovered powder fire extinguishing agent charged into the first stage sieve 2A is mixed with foreign parts such as fire extinguisher parts, factory waste containing magnetic metal, and dust. Large foreign matters such as fire extinguisher parts and factory waste materials containing magnetic metals can be captured by the first stage sieve 2A and separated from unused recovered powder fire extinguishing agents.
[0015]
The unused recovered powder extinguishing agent that has passed through the first-stage sieve 2A is sent to the second-stage sieve 2B. The unused recovered powder extinguishing agent sent to the second stage sieve 2B is smaller than the large foreign matter captured and separated and removed by the first stage sieve 2A. Medium-sized foreign matter such as factory waste and garbage containing magnetic metal that is sufficiently larger than that. These medium-sized foreign substances can be captured by the second stage sieve 2B and separated and removed from the unused recovered powder fire extinguishing agent.
[0016]
The first stage sieve 2A separates and removes foreign matter such as large fire extinguisher parts and factory waste containing magnetic metal, thereby greatly reducing the gravity applied to the second stage sieve 2B. Therefore, even if the second stage sieve 2B has a structure with a thin wire diameter having a mesh number of about 50 mesh, an appropriate sieve is executed by avoiding the spread of the line by the medium-sized foreign matter or the mesh damage. be able to.
[0017]
The unused recovered powder extinguishing agent that has passed through the second stage sieve 2B is sent to the third stage sieve 2C. The unused recovered powder extinguishing agent sent to the third stage sieve 2C is smaller than the medium-sized foreign matter captured and separated and removed by the second stage sieve 2B, and the particles of unused recovered powder extinguishing agent Fine foreign matter such as factory waste and dust containing magnetic metal slightly larger than the diameter is mixed. These fine foreign substances can be captured and removed from the unused recovered powder fire extinguishing agent by the third stage sieve 2C. That is, fine foreign matters such as factory waste and dust containing magnetic metal having a particle diameter exceeding 83 mesh can be captured and separated from unused recovered powder fire extinguishing chemicals.
[0018]
Since the foreign material such as the medium-sized fire extinguisher parts and the factory waste material in the foreign material is separated and removed by the second stage fluid 2B, the gravity applied to the third stage fluid 2C is further reduced, so that the third stage Even if the mesh 2C of the mesh has a mesh size of 83 mesh and an extremely fine wire diameter, it is possible to avoid the spread of the wire and damage to the mesh due to a fine foreign substance, and to execute an appropriate sieve.
[0019]
The unused recovered powder extinguishing agent that has passed through the third stage sieve 2C has a particle size that is not more than the standard particle size (83 mesh) defined by the national certification standard. The unused recovered powder extinguisher that has passed through the third stage sieve 2C is sent to the magnetic adsorption device 3 equipped with a permanent magnet or an electromagnet. Here, the third stage sieve 2C is used together with the unused recovered powder extinguisher. The passed magnetic metal (magnetic metal powder) is removed by adsorption.
[0020]
The unused recovered powder extinguishing agent from which the magnetic metal powder has been adsorbed and removed by passing through the magnetic adsorption device 3 is batched by adding 100 kg to the batch tank 4 and sampled from the batched unused recovered powder extinguishing agent. Extraction of air bubbles to check for bubble generation, pressure test to check pressure rise, gas analysis to check for gas generation, color test with color meter, pH test with pH meter, etc. If foreign matter such as collected powder fire extinguishing agent (BC powder) or soil is found to be mixed, the batch of unused recovered powder extinguishing agent equivalent to 100 kg is discarded, and different unused recovered powder extinguishing agent (BC powder) ) And soil and other foreign matter is not observed, the white carbon coated with silicon is separated and removed by a separating device 5 such as a classification rotor, and phosphoric acid An unused recovered powder fire extinguisher mainly composed of nickel and ammonium sulfate is put into the batch tank 6, a sample is extracted from the unused recovered powder fire extinguisher, and ammonium phosphate and ammonium sulfate are extracted by an X-ray diffraction analyzer. Measure the ratio and store 500 kg of unused recovered powder fire extinguishing agent measured by the balance weighing device 7 in one container pack, and use the unused recovered powder extinguishing agent stored in the container pack as a reusable raw material. Can do. The ratio of ammonium phosphate and ammonium sulfate measured by the X-ray diffraction analyzer is a guideline for the replenishment amount of new ammonium phosphate and ammonium sulfate to be replenished when unused recovered powder fire extinguishing agent is used as a reuse material. Become.
[0021]
In the above-described embodiment, the sieve is separated by the sieve separator 2 having the three-stage sieves 2A, 2B, and 2C in which one sieve 2B is arranged between the first-stage sieve 2A and the final-stage sieve 2C. Although the above-described method is used, the method is such that a sieve is applied by a sieve separator 2 having four or more stages of sieves in which a plurality of sieves are arranged between the first stage sieve 2A and the final stage sieve 2C. May be.
[0022]
【The invention's effect】
As described above, since the method for separating and recovering unused recovered powder fire extinguishing agents according to the present invention is configured, the following special effects are achieved.
[0023]
According to the first aspect of the present invention, the unused powder fire extinguishing agent is easily separated from the unused powder fire extinguishing agent, which is transferred to the receiving container such as a one-dot can. Only the drug can be reliably recovered and used as a recycled material . Furthermore, by adsorbing and removing the magnetic metal (magnetic metal powder) that has passed through the final stage sieve together with the unused recovered powder fire extinguisher, it is possible to avoid a decrease in the purity of the unused powder fire extinguisher that can be used as a recycled material. .
[0024]
According to the second aspect of the present invention, it is possible not only to recover unused powder fire extinguishing agent that can be used as a recycle raw material having a particle size equal to or less than a reference particle size (83 mesh), but also to recover unused recovered powder fire extinguishing. Gravity applied to the fluid in the subsequent stage is reduced by separating and removing from large foreign substances mixed with chemicals to fine foreign substances, thereby avoiding the spread of lines and damage to meshes due to foreign substances. Thus, it is possible to contribute to the execution of an appropriate fluid.
[0025]
[Brief description of the drawings]
FIG. 1 is a flowchart applied to an embodiment of the present invention.
[Explanation of symbols]
2 Fluid separator 2A First stage fluid 2C Third stage fluid (final stage fluid)
3 Magnetic adsorption device

Claims (2)

消火器から抜き出した未使用回収粉末消火薬剤を受入容器に移し、この未使用回収粉末消火薬剤を、1段目の篩(以下、フルイという)から最終段のフルイにかけて網目数が増加する複数段のフルイを備えたフルイ分離装置に投入してフルイ分離処理を施し、前記最終段のフルイを通過することで前記フルイ分離処理された未使用回収粉末消火薬剤から磁気吸着装置により磁性金属を吸着除去することを特徴とする未使用回収粉末消火薬剤の分離回収方法。Move the unused recovered powder fire extinguisher extracted from the fire extinguisher to a receiving container, and then add this unused recovered powder fire extinguisher from the first stage sieve (hereinafter referred to as “fluid”) to the final stage sieve. and facilities the sieve separation process was put into sieve separator with a sieve, adsorption to magnetic metal by the magnetic adsorption device from the unused recovered powder fire extinguishing agent, which is the sieve separation process by passing through a sieve of the last stage A method for separating and recovering unused recovered powder fire extinguishing agent, characterized in that it is removed . 前記1段目のフルイの目開きが1〜5cmに設定され、最終段のフルイの網目数が83メッシュに設定されている請求項1に記載の未使用回収粉末消火薬剤の分離回収方法。  The method for separating and collecting unused recovered powder fire extinguishing agent according to claim 1, wherein the opening of the first stage sieve is set to 1 to 5 cm, and the number of meshes of the final stage sieve is set to 83 mesh.
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KR101978851B1 (en) * 2018-07-25 2019-05-16 주식회사 소방 119 Recycling system for dry chemical powder of old extinguisher
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