JPS6127863Y2 - - Google Patents

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Publication number
JPS6127863Y2
JPS6127863Y2 JP418381U JP418381U JPS6127863Y2 JP S6127863 Y2 JPS6127863 Y2 JP S6127863Y2 JP 418381 U JP418381 U JP 418381U JP 418381 U JP418381 U JP 418381U JP S6127863 Y2 JPS6127863 Y2 JP S6127863Y2
Authority
JP
Japan
Prior art keywords
powder
transport
gas
valve
pressure tank
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP418381U
Other languages
Japanese (ja)
Other versions
JPS57116625U (en
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed filed Critical
Priority to JP418381U priority Critical patent/JPS6127863Y2/ja
Publication of JPS57116625U publication Critical patent/JPS57116625U/ja
Application granted granted Critical
Publication of JPS6127863Y2 publication Critical patent/JPS6127863Y2/ja
Expired legal-status Critical Current

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  • Auxiliary Methods And Devices For Loading And Unloading (AREA)
  • Air Transport Of Granular Materials (AREA)

Description

【考案の詳細な説明】 本考案は、食品、医薬品、化粧品等の粉粒体の
輸送装置に関するものである。
[Detailed Description of the Invention] The present invention relates to an apparatus for transporting powdery materials such as foods, medicines, cosmetics, etc.

食品、医薬品、化粧品等の粉粒体原料は、防
疫、減菌のためにガスくん蒸による処置が法的に
義務づけられ、あるいは自主的に実施されてい
る。それで、本考案は通常使用されている圧力タ
ンク式空気輸送装置を利用して、ガスくん蒸を効
果的に行うと共に、くん蒸処理後の粉粒体を輸送
できる装置を提供することを目的として開発され
たものである。
Powdered raw materials for foods, pharmaceuticals, cosmetics, etc. are legally required or voluntarily treated with gas fumigation for epidemic prevention and sterilization purposes. Therefore, the present invention was developed with the aim of providing a device that can effectively perform gas fumigation and transport powder and granular materials after fumigation using a commonly used pressure tank type pneumatic transportation device. It is something that

以下、本考案を添付する図面に示す具体的な実
施例に基いて詳細に説明する。
Hereinafter, the present invention will be described in detail based on specific embodiments shown in the accompanying drawings.

第1図において、圧力タンク1の上方に受入弁
2を介して粉粒体を収容する仮貯蔵タンク3を設
置する。真空ポンプ4はフイルター5、真空弁6
を介して真空配管7により圧力タンク1に接続
し、真空ポンプ4にはくん蒸ガスを無毒化処理す
るための中和装置8を接続する。真空ポンプ4を
駆動することにより圧力タンク1内を真空状態と
し、圧力タンク1に設けた真空スイツチ9の予め
設定した真空圧により真空弁6を閉じる。輸送ガ
ス源10は減菌フイルター11および輸送ガス弁
12を介して配送ガス配管13により圧力タンク
1の最下部に接続する。圧力タンク1内の下部に
は取扱う粉粒体の粒子より小径の多数の通気孔を
穿設した散気板14を設け、粉粒体の輸送管15
を受入口16を散気板14の上方に位置せしめ圧
力タンク1内に垂設し上方を屈曲させて圧力タン
ク1の側壁から突出させ輸送弁17を介在させ
る。メチールブロマイドCH3Br等のくん蒸ガス源
18はくん蒸ガス弁19を介してくん蒸配管20
により輸送ガス配管13に接続する。圧力タンク
1内の上部には圧力タンク1内の圧力を検知する
圧力スイツチ21を設ける。
In FIG. 1, a temporary storage tank 3 is installed above a pressure tank 1 via a receiving valve 2 to accommodate powder and granular material. Vacuum pump 4 includes filter 5 and vacuum valve 6
It is connected to the pressure tank 1 via a vacuum pipe 7, and the vacuum pump 4 is connected to a neutralization device 8 for detoxifying fumigation gas. By driving the vacuum pump 4, the inside of the pressure tank 1 is brought into a vacuum state, and the vacuum valve 6 is closed by a preset vacuum pressure of a vacuum switch 9 provided in the pressure tank 1. A transport gas source 10 is connected to the lowest part of the pressure tank 1 by a delivery gas line 13 via a sterile filter 11 and a transport gas valve 12 . At the lower part of the pressure tank 1, there is provided an air diffuser plate 14 with a large number of ventilation holes having a diameter smaller than that of the particles of powder and granular material to be handled.
The intake port 16 is positioned above the air diffuser plate 14, and is vertically provided in the pressure tank 1, with the upper part bent to protrude from the side wall of the pressure tank 1, and the transport valve 17 is interposed therebetween. A fumigation gas source 18 such as methyl bromide CH 3 Br is connected to a fumigation pipe 20 via a fumigation gas valve 19 .
It is connected to the transport gas piping 13 by. A pressure switch 21 is provided at the upper part of the pressure tank 1 to detect the pressure inside the pressure tank 1.

この装置の作用について説明する。まず、仮貯
蔵タンク3に収容された未処理の粉粒体Pを受入
弁2を開き所定量圧力タンク1内に受入れる。次
に粒体粒子の空隙の空気ができるだけくん蒸ガス
と置換するように、受入弁2、くん蒸ガス弁1
9、輸送ガス弁12および輸送弁17を閉じ、真
空弁6を開き、真空ポンプ4を駆動してフイルタ
ー5、真空弁6、真空配管7を経て圧力タンク1
内の空気を抜き出して真空状態とし、圧力タンク
1が真空スイツチ9で設定した圧力になると真空
スイツチ9で検知して真空弁6を閉じる。次に、
くん蒸ガス源18を駆動すると共にくん蒸ガス弁
19を開き、くん蒸ガスはくん蒸ガス弁19、く
ん蒸配管20および輸送ガス配管13を経て圧力
タンク1内の最下部に至り散気板14を経て圧力
タンク1内に流入し、圧力タンク1内の粉粒体P
を激しく撹拌すると共に粉粒体Pの粒子間の微小
な空間まで空気を置換して高い濃度で浸入し殺
菌、殺虫を行う。くん蒸ガスは圧力スイツチ21
が設定した圧力まで加圧し、くん蒸弁19を閉じ
てくん蒸効果に必要な予め設定した時間、圧力タ
ンク1内に滞留する。くん蒸時間が終了すると、
真空弁6を開きくん蒸ガスは無毒化処理のため真
空配管7、真空弁6からフイルター5を経て粉粒
体Pを過し、中和装置8に導入し安全な排気ガ
スとして系外へ放出する。系内が略大気圧状態に
なると、再び真空ポンプ4を駆動して圧力タンク
1内の粉粒体P内に残留するくん蒸ガスを排出
し、圧力タンク1の圧力が真空スイツチ9で設定
した真空圧になるまで排気すると真空弁6を閉
じ、別系からの粉粒体Pの輸送指令を待つ。輸送
指令が来ると、輸送ガス源10を駆動すると共に
輸送ガス弁12を開き、輸送ガスは減菌フイルタ
ー11を経て清浄化し、輸送ガス弁12、輸送ガ
ス配管13を経て圧力タンク1内の最下部に至
り、散気板14を経て圧力タンク1内に流入し粉
粒体Pを撹拌し昇圧する。輸送ガスが圧力スイツ
チ21の設定圧力になると、輸送弁17を開き粉
粒体Pは輸送ガスとの固気混合流となつて輸送管
15に受入口16より流入し輸送弁17を経て輸
送先に圧送される。圧力タンク1内の粉粒体Pが
なくなつたことを圧力スイツチ21の下限圧力ま
たは図示してない下限粉面計や重量測定装置等で
検知した後、輸送弁17および輸送ガス弁12を
閉じ輸送ガス源10の駆動を停止する。このよう
にしてこの装置の1サイクルの駆動を停止する。
The operation of this device will be explained. First, the receiving valve 2 is opened to receive a predetermined amount of unprocessed powder P stored in the temporary storage tank 3 into the pressure tank 1. Next, the intake valve 2, the fumigation gas valve 1
9. Close the transport gas valve 12 and the transport valve 17, open the vacuum valve 6, and drive the vacuum pump 4 to supply the pressure tank 1 through the filter 5, vacuum valve 6, and vacuum piping 7.
The air inside is extracted to create a vacuum state, and when the pressure in the pressure tank 1 reaches the pressure set by the vacuum switch 9, the vacuum switch 9 detects this and closes the vacuum valve 6. next,
The fumigation gas source 18 is driven and the fumigation gas valve 19 is opened, and the fumigation gas passes through the fumigation gas valve 19, the fumigation pipe 20, and the transport gas pipe 13, reaches the lowest part of the pressure tank 1, passes through the diffuser plate 14, and enters the pressure tank. 1 and the powder P in the pressure tank 1
At the same time, the powder P is vigorously stirred and air is displaced into the minute spaces between the particles of the powder P to infiltrate at a high concentration to sterilize and kill insects. Pressure switch 21 for fumigation gas
is pressurized to a preset pressure, the fumigation valve 19 is closed, and the sample remains in the pressure tank 1 for a preset time necessary for the fumigation effect. When the fumigation time is over,
The vacuum valve 6 is opened, and the fumigation gas is detoxified through the vacuum piping 7, the vacuum valve 6, the filter 5, the powder P, and then introduced into the neutralization device 8, where it is released outside the system as a safe exhaust gas. . When the inside of the system reaches approximately atmospheric pressure, the vacuum pump 4 is driven again to exhaust fumigation gas remaining in the powder P in the pressure tank 1, and the pressure in the pressure tank 1 becomes the vacuum set by the vacuum switch 9. Once the pressure is reached, the vacuum valve 6 is closed and a command to transport the powder P from another system is awaited. When a transport command is received, the transport gas source 10 is driven and the transport gas valve 12 is opened, and the transport gas is purified through the sterilization filter 11, passed through the transport gas valve 12 and the transport gas piping 13, and is then sent to the top of the pressure tank 1. It reaches the lower part, flows into the pressure tank 1 through the air diffuser plate 14, stirs the powder P, and increases the pressure. When the transport gas reaches the set pressure of the pressure switch 21, the transport valve 17 is opened, and the powder P becomes a solid-gas mixed flow with the transport gas, flows into the transport pipe 15 from the intake port 16, passes through the transport valve 17, and is transported to the destination. will be pumped to. After detecting that the powder P in the pressure tank 1 is gone is detected by the lower limit pressure of the pressure switch 21 or by a lower limit powder meter or weight measuring device (not shown), the transport valve 17 and the transport gas valve 12 are closed. Stop driving the transport gas source 10. In this way, one cycle of driving of this device is stopped.

第2図および第3図は本考案の第2および第3
の実施例で、第1図の第1実施例と同一の機能を
有するものは同一の符号を付して示す。フイルタ
5と駆動源となる真空ポンプと輸送ガス源となる
ガス圧縮装置の機能を兼備した真空圧縮両用装置
22と減菌フイルター11とを弁23,24,2
5,26を介在させ直列に接続し、フイルター5
を圧力タンク1の上部に減菌フイルター11を最
下部に接続し、くん蒸ガス源18を弁23に中和
装置8を弁25にそれぞれ接続し、第3実施例で
は圧力タンク1への仮貯蔵タンク3からの粉粒体
Pの供給を真空輸送でなす圧力タンク1と仮貯蔵
タンク3とを隔てて設置したものである。
Figures 2 and 3 are the second and third diagrams of the present invention.
In this embodiment, parts having the same functions as those of the first embodiment shown in FIG. 1 are denoted by the same reference numerals. The filter 5, a vacuum compression device 22 that has the functions of a vacuum pump serving as a drive source, and a gas compression device serving as a transport gas source, and a sterilization filter 11 are connected to valves 23, 24, 2.
Filters 5 and 26 are connected in series with filters 5 and 26 interposed in between.
is connected to the upper part of the pressure tank 1 and the sterilization filter 11 is connected to the bottom part, the fumigation gas source 18 is connected to the valve 23, the neutralization device 8 is connected to the valve 25, and in the third embodiment, temporary storage in the pressure tank 1 is performed. A pressure tank 1 and a temporary storage tank 3 are installed to be separated from each other by vacuum transporting the powder P from the tank 3.

真空動作時およびくん蒸ガス排気時には圧力タ
ンク1からフイルター5、真空圧縮両用装置2
2、中和装置8の方向に流通するように弁操作
し、くん蒸動作時にはくん蒸ガス源18から真空
圧縮両用装置22、減菌フイルター11、圧力タ
ンク1の方向に、輸送動作時は大気から真空圧縮
両用装置22、減菌フイルター11、圧力タンク
1、輸送管15の方向にそれぞれ流通するように
弁操作する。また、第3実施例では真空動作によ
り仮貯蔵タンク3に収容された粉粒体Pを圧力タ
ンク1に供給するように弁操作する。
During vacuum operation and fumigation gas exhaust, pressure tank 1 to filter 5, vacuum compression device 2
2. Operate the valve so that it flows in the direction of the neutralization device 8, and during fumigation operation, from the fumigation gas source 18 to the vacuum compression device 22, sterilization filter 11, and pressure tank 1, and from the atmosphere to the vacuum during transportation operation. The valves are operated to flow in the directions of the compression dual-purpose device 22, the sterilization filter 11, the pressure tank 1, and the transport pipe 15, respectively. Further, in the third embodiment, the valve is operated so that the powder P stored in the temporary storage tank 3 is supplied to the pressure tank 1 by vacuum operation.

本考案は、叙上のように、圧力タンクに、粉粒
体を収容する仮貯蔵タンク、真空ポンプ、くん蒸
ガス源、輸送ガス源および輸送管を弁を介在させ
てそれぞれ接続し、該圧力タンクに対して各弁を
開閉して、粉粒体を所定量受入れ、粒体粒子間の
空気を抜き出し真空状態にし、くん蒸ガスを流入
させて空気と置換すると共に粉粒体を撹拌し、く
ん蒸ガスを排出し、輸送ガスを流入させて粉粒体
を輸送管より圧送させるように構成した粉粒体輸
送装置であり、食品、医薬品、化粧品等の粉粒体
原料のくん蒸を効果的に行うと共にくん蒸処理後
の粉粒体の輸送が可能である。
As described above, the present invention connects a temporary storage tank containing powder and granules, a vacuum pump, a fumigation gas source, a transport gas source, and a transport pipe to a pressure tank through valves, and the pressure tank Each valve is opened and closed to receive a predetermined amount of powder and granules, the air between the granules is removed to create a vacuum state, fumigation gas is introduced to replace the air, and the powder is stirred to remove the fumigation gas. This is a powder transport device configured to discharge powder and transport gas and forcefully transport the powder through the transport pipe. It is possible to transport powdered materials after fumigation treatment.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本考案の一実施例を示す図、第2図は
本考案の第2実施例を示す図、第3図は本考案の
第3実施例を示す図である。 1……圧力タンク、P……粉粒体、3……仮貯
蔵タンク、4……真空ポンプ、22……真空圧縮
両用装置、18……くん蒸ガス源、10……輸送
ガス源、15……輸送管、2,6,19,12,
17,23,24,25,26……弁。
FIG. 1 is a diagram showing an embodiment of the invention, FIG. 2 is a diagram showing a second embodiment of the invention, and FIG. 3 is a diagram showing a third embodiment of the invention. 1... Pressure tank, P... Powder, 3... Temporary storage tank, 4... Vacuum pump, 22... Vacuum compression dual use device, 18... Fumigation gas source, 10... Transportation gas source, 15... ...transport pipe, 2, 6, 19, 12,
17, 23, 24, 25, 26... valve.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 圧力タンクに、粉粒体を収容する仮貯蔵タン
ク、真空ポンプ、くん蒸ガス源、輸送ガス源およ
び輸送管を弁を介在させてそれぞれ接続し、該圧
力タンクに対して各弁を開閉して、粉粒体を所定
量受入れ、粉体粒子間の空気を抜き出し真空状態
にし、くん蒸ガスを流入させて空気と置換すると
共に粉粒体を撹拌し、くん蒸ガスを排出し、輸送
ガスを流入させて粉粒体を輸送管より圧送させる
ように構成したことを特徴とする粉粒体輸送装
置。
A temporary storage tank containing powder and granular material, a vacuum pump, a fumigation gas source, a transport gas source, and a transport pipe are connected to the pressure tank through valves, and each valve is opened and closed with respect to the pressure tank, Accepts a predetermined amount of powder and granules, extracts the air between the powder particles to create a vacuum state, introduces fumigation gas to replace the air, stirs the powder, discharges the fumigation gas, and allows transport gas to flow in. A powder and granule transport device characterized by being configured to forcefully transport powder and granules through a transport pipe.
JP418381U 1981-01-13 1981-01-13 Expired JPS6127863Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP418381U JPS6127863Y2 (en) 1981-01-13 1981-01-13

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP418381U JPS6127863Y2 (en) 1981-01-13 1981-01-13

Publications (2)

Publication Number Publication Date
JPS57116625U JPS57116625U (en) 1982-07-20
JPS6127863Y2 true JPS6127863Y2 (en) 1986-08-19

Family

ID=29802616

Family Applications (1)

Application Number Title Priority Date Filing Date
JP418381U Expired JPS6127863Y2 (en) 1981-01-13 1981-01-13

Country Status (1)

Country Link
JP (1) JPS6127863Y2 (en)

Also Published As

Publication number Publication date
JPS57116625U (en) 1982-07-20

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