JP2001130744A - Powder and granular material transfer device and water treatment facility using powder and granular material transfer device - Google Patents

Powder and granular material transfer device and water treatment facility using powder and granular material transfer device

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Publication number
JP2001130744A
JP2001130744A JP31527099A JP31527099A JP2001130744A JP 2001130744 A JP2001130744 A JP 2001130744A JP 31527099 A JP31527099 A JP 31527099A JP 31527099 A JP31527099 A JP 31527099A JP 2001130744 A JP2001130744 A JP 2001130744A
Authority
JP
Japan
Prior art keywords
powder
granular material
transfer device
air
material transfer
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.)
Granted
Application number
JP31527099A
Other languages
Japanese (ja)
Other versions
JP3420140B2 (en
Inventor
Shunichi Yoshimoto
俊一 吉元
Hisafumi Shinohara
久文 篠原
Takahiro Suzuki
隆洋 鈴木
Noriyuki Matsunobu
紀至 松延
Hiroshi Motohashi
寛 本橋
Yosuke Takashima
洋介 高嶋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ebara Corp
Original Assignee
Ebara Corp
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 by Ebara Corp filed Critical Ebara Corp
Priority to JP31527099A priority Critical patent/JP3420140B2/en
Publication of JP2001130744A publication Critical patent/JP2001130744A/en
Application granted granted Critical
Publication of JP3420140B2 publication Critical patent/JP3420140B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide a powder and granular material transfer device capable of smoothly transferring powder and granular materials cut out from a powder and granular material storage tank without generating clogging by uniformly mixing the powder and granular materials with air and capable of transferring them to a plurality of target places. SOLUTION: In a powder and granular material transfer device, a mixing tank 12 having an air inflow port 13 and a mixture outflow ports 14, 15 is arranged on the lower end of a powder and granular material storage tank 11, powder and granular materials C cut out from the powder and granular material storage tank 11 and air A flowing from the air inflow port 13 are mixed with each other in the mixing tank 12, and the powder and granular materials mixed with air are transferred from the mixture outflow ports 14, 15 to specified places through transfer pipes. The transfer pipes 17, 18 are connected to a plurality of mixture outflow ports 14, 15 to transfer powder and granular materials to a plurality of target places.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、粉粒体移送装置に
関し、例えば水処理の設備で用いる活性炭(ドライ炭)
・消石灰、乾燥汚泥等の粉粒体を所定の場所に移送する
粉粒体移送装置及び該粉粒体移送装置を用いた水処理設
備に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a granular material transfer device, and more particularly to activated carbon (dry carbon) used in water treatment equipment.
The present invention relates to a powder and granule transfer device for transferring powder and granules such as slaked lime and dried sludge to a predetermined place, and to a water treatment facility using the powder and granule transfer device.

【0002】[0002]

【従来の技術】水処理設備の沈砂池、着水井等におい
て、通常の浄水処理で除去できない異臭味原因物質、ト
リハロメタン及びその前駆物質、その他の有機物等を除
去するために、水分5%以下のドライ活性炭の注入が行
われている。このドライ活性炭を注入場所に移送するの
に、粉塵の飛散等の防止及び移送効率の観点から粉粒体
移送管を用いて、加圧方式又は吸引方式で空気により目
的場所に移送する方法が行われている。
2. Description of the Related Art In sedimentation basins and landing wells of water treatment facilities, to remove off-flavor-causing substances, trihalomethane and its precursors, and other organic substances that cannot be removed by ordinary water purification treatment, the water content is 5% or less. Dry activated carbon is being injected. In order to prevent the scattering of dust and transfer efficiency, a method of transferring the dry activated carbon to the injection place by air using a powder transfer pipe or a pressurized method or a suction method by air is used. Have been done.

【0003】図1は従来のこの種の粉粒体移送装置の概
略構成を示す図である。図1において、1は活性炭や消
石灰等の粉粒体を収容する粉粒体貯留槽であり、該粉粒
体貯留槽1の下方には粉粒体切出機2が設けられ、該粉
粒体切出機2の下端に移送管3が配置されている。
FIG. 1 is a diagram showing a schematic configuration of a conventional powder and granular material transfer apparatus of this kind. In FIG. 1, reference numeral 1 denotes a granular material storage tank for storing a granular material such as activated carbon or slaked lime, and a granular material extracting device 2 is provided below the granular material storage tank 1; A transfer pipe 3 is arranged at a lower end of the body extractor 2.

【0004】上記構成の粉粒体移送装置において、粉粒
体切出機2によって粉粒体貯留槽1から移送管3内に切
出された粉粒体は、加圧空気又は吸引空気により、矢印
Aに示す方向に空気と混合した状態で移送される。
[0004] In the granular material transfer apparatus having the above structure, the granular material cut out from the granular material storage tank 1 into the transfer pipe 3 by the granular material cutting device 2 is compressed or sucked air. It is transported in a direction indicated by arrow A while being mixed with air.

【0005】しかしながら、上記従来構成の粉粒体移送
装置においては、粉粒体切出機2の直下部で移送する粉
粒体と空気の混合を均一とすることが難しく、粉粒体切
出機2の直下において、粉粒体による目詰まりが発生し
易いという問題があった。また、構造的に複数の粉粒体
移送管を設け、複数の目的場所に粉粒体を移送できるよ
うに構成することが難しいという問題もあった。
However, in the above-described conventional granular material transfer apparatus, it is difficult to make the mixing of the granular material transferred directly below the granular material cutting machine 2 and the air uniform, so that the granular material cut-out device is not used. There is a problem that clogging by the granular material easily occurs immediately below the machine 2. There is also a problem that it is difficult to structurally provide a plurality of granular material transfer pipes so as to transfer the granular material to a plurality of destinations.

【0006】[0006]

【発明が解決しようとする課題】本発明は上述の点に鑑
みてなされたもので、粉粒体貯留槽から切出された粉粒
体を空気と均一に混合させ、目詰まりを発生することな
くスムーズに移送できる粉粒体移送装置及び該粉粒体移
送装置を用いた水処理設備を提供することを目的とす
る。
DISCLOSURE OF THE INVENTION The present invention has been made in view of the above points, and it is an object of the present invention to uniformly mix powder and granular material cut out from a granular material storage tank with air to cause clogging. It is an object of the present invention to provide a powder and granular material transfer device that can smoothly transfer without any trouble, and a water treatment facility using the powder and particle material transfer device.

【0007】また、粉粒体貯留槽から切出された粉粒体
を空気と均一に混合させ、同時に複数の目的場所に移送
させることができる粉粒体移送装置及び該粉粒体移送装
置を用いた水処理設備を提供することを目的とする。
Further, the present invention provides a powder / particle transfer apparatus and a powder / particle transfer apparatus capable of uniformly mixing powder / particles cut out from a powder / particle storage tank with air and simultaneously transferring the powder / particles to a plurality of destinations. The purpose is to provide the used water treatment equipment.

【0008】[0008]

【課題を解決するための手段】上記課題を解決するため
請求項1に記載の発明は、粉粒体を貯留する粉粒体貯留
槽、該粉粒体貯留槽の下部に配置した移送管を具備し、
粉粒体貯留槽から切出機で切出した粉粒体を該移送管で
空気により加圧方式或いは吸引方式にて移送する粉粒体
移送装置において、粉粒体貯留槽の下端に空気流入口、
混合体流出口を有する混合槽を配備し、該混合槽で粉粒
体貯留槽から切出された粉粒体と空気流入口から流入し
た空気とを混合し、混合体流出口から移送管を通して空
気と混合した粉粒体を所定の場所に移送することを特徴
とする。
According to a first aspect of the present invention, there is provided a powder and granule storage tank for storing powder and granules, and a transfer pipe disposed below the powder and granule storage tank. Have,
An air inlet at the lower end of the granular material storage tank in a granular material transfer device for transferring the granular material cut out from the granular material storage tank by a cutting machine using the transfer pipe by air using a pressurizing method or a suction method. ,
A mixing tank having a mixture outlet is provided, and the powder and granules cut out from the powder storage tank and the air flowing in from the air inlet are mixed in the mixing tank, and the mixture is passed through the transfer pipe from the mixture outlet. It is characterized in that the granules mixed with air are transferred to a predetermined place.

【0009】上記のように粉粒体貯留槽の下端に混合槽
を配備することにより、粉粒体貯留槽から切出された粉
粒体は該混合槽内で空気と均一に混合される。これによ
り粉粒体は目詰まりを発生することなく、移送管を通っ
て所定の場所に移送される。
By disposing the mixing tank at the lower end of the powder storage tank as described above, the powder cut out from the powder storage tank is uniformly mixed with air in the mixing tank. As a result, the granular material is transferred to a predetermined place through the transfer pipe without causing clogging.

【0010】また、請求項2に記載の発明は、請求項1
に記載の粉粒体移送装置において、空気流入口及び混合
体流出口に断面積の小さい収縮部を設けたことを特徴と
する。
[0010] The invention described in claim 2 is the same as the claim 1.
Wherein the shrinking portion having a small cross-sectional area is provided at the air inlet and the mixture outlet.

【0011】上記のように空気流入口及び混合体流出口
に収縮部を設けたことにより、混合槽内に流入する空気
の流速を速めることができ、この流速の速い空気が混合
槽内で速い旋回流を発生するから、混合槽内に流入した
粉粒体はこの旋回流により空気と均一に混合する。ま
た、空気と粉粒体の混合体も混合体流出口の収縮部を通
って高速で移送管内に噴出される。その結果、粉粒体を
目詰まりを発生させることなく、スムーズに移送でき
る。
As described above, the provision of the contraction portions at the air inlet and the mixture outlet allows the flow velocity of the air flowing into the mixing tank to be increased, and the air having the high flow velocity is increased in the mixing tank. Since a swirling flow is generated, the powder and granules flowing into the mixing tank are uniformly mixed with air by the swirling flow. A mixture of air and powder is also ejected at a high speed into the transfer pipe through the contracted portion of the mixture outlet. As a result, the powders can be smoothly transferred without causing clogging.

【0012】また、請求項3に記載の発明は、請求項1
又は2に記載の粉粒体移送装置において、混合槽には複
数個の混合体流出口が設けられ、該複数の混合体流出口
のそれぞれに粉粒体移送管を接続したことを特徴とす
る。
Further, the invention described in claim 3 is the first invention.
Alternatively, in the powder and granular material transfer device according to 2, a plurality of mixture outlets are provided in the mixing tank, and a powder and particle transfer pipe is connected to each of the plurality of mixture outlets. .

【0013】上記のように混合槽に複数個の混合体流出
口を設け、該混合体流出口のそれぞれに粉粒体移送管を
接続するので、複数の目的場所に粉粒体を移送すること
ができる。
As described above, a plurality of mixture outlets are provided in the mixing tank, and the powder transfer pipes are connected to each of the mixture outlets, so that the powder can be transferred to a plurality of destinations. Can be.

【0014】また、請求項4に記載の発明は、粉粒体を
所定の場所から所定の場所へ移送する粉粒体移送装置を
具備する水処理設備において、粉粒体移送装置に請求項
1乃至3のいずれか1項に記載の粉粒体移送装置を用い
ることを特徴とする。
According to a fourth aspect of the present invention, there is provided a water treatment facility having a granular material transfer device for transferring a granular material from a predetermined location to a predetermined location. 4. The apparatus for transferring a granular material according to any one of the above items 3 to 3.

【0015】上記のように水処理設備の粉粒体移送装置
に請求項1乃至3のいずれか1項に記載の粉粒体移送装
置を用いることにより、効率よく活性炭、消石灰、乾燥
汚泥等の粉粒体を所定の場所から所定の場所に移送する
ことができ、水処理の効率を向上させることができる。
As described above, by using the granular material transfer device according to any one of claims 1 to 3 for a granular material transfer device of a water treatment facility, activated carbon, slaked lime, dried sludge and the like can be efficiently used. The granular material can be transferred from a predetermined place to a predetermined place, and the efficiency of water treatment can be improved.

【0016】[0016]

【発明の実施の形態】以下、本発明の実施の形態例を図
面に基づいて説明する。図2は本発明に係る粉粒体移送
装置の概略構成を示す図である。本粉粒体移送装置は、
粉粒体を貯留する粉粒体貯留槽11の下部に混合槽12
を配置している。該混合槽12には空気流入口13と複
数個(図では2個)の混合体流出口14、15が設けら
れている。空気流入口13は空気管16が接続され、混
合体流出口14、15にはそれぞれ移送管17、18が
接続される。粉粒体貯留槽11と混合槽12の間には粉
粒体切出機19が配置されている。また、空気流入口1
3、混合体流出口14、15にはそれぞれ断面積を小さ
くする収縮部13a、14a、15aが設けられてい
る。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 2 is a diagram showing a schematic configuration of the granular material transfer device according to the present invention. This granular material transfer device is
A mixing tank 12 is provided at a lower portion of the powder material storage tank 11 for storing the powder material.
Has been arranged. The mixing tank 12 is provided with an air inlet 13 and a plurality (two in the figure) of mixture outlets 14 and 15. The air inlet 13 is connected to an air pipe 16, and the mixture outlets 14 and 15 are connected to transfer pipes 17 and 18, respectively. A granular material cutting machine 19 is disposed between the granular material storage tank 11 and the mixing tank 12. The air inlet 1
3. The mixture outlets 14 and 15 are provided with shrinking portions 13a, 14a and 15a, respectively, for reducing the cross-sectional area.

【0017】上記構成の粉粒体移送装置において、混合
槽12内には空気管16を通して空気Aが空気流入口1
3から加圧方式或いは吸引方式で流入する。該空気Aは
混合槽内で矢印Bに示すように渦巻状に旋回する。一
方、粉粒体貯留槽11から粉粒体切出機19で切出され
た粉粒体Cは混合槽12の頂部から流入し、該混合槽1
2内で空気Aと混合し、混合体流出口14、15から移
送管17、18内に流出する。移送管17、18はそれ
ぞれそ粉粒体を移送する目的場所にまで延びており、混
合槽12内で空気と混合した粉粒体は目的場所まで移送
される。
In the apparatus for transferring powdery and granular materials having the above structure, air A flows into the mixing tank 12 through the air pipe 16.
3 flows in by a pressure method or a suction method. The air A swirls in the mixing tank as shown by arrow B. On the other hand, the granular material C cut out from the granular material storage tank 11 by the granular material cutting machine 19 flows in from the top of the mixing tank 12, and the mixing tank 1
It mixes with air A in 2 and flows out of mixture outlets 14 and 15 into transfer pipes 17 and 18. The transfer pipes 17 and 18 respectively extend to the destination where the powder is transferred, and the powder mixed with air in the mixing tank 12 is transferred to the destination.

【0018】混合槽12の空気流入口13には上記のよ
うに収縮部13aが設けられており、空気管16内の空
気Aの流速(例えば10m/s)は該収縮部13aを通
ることにより速められ(例えば20〜30m/s)、噴
流となって混合槽12内に流入するから、混合槽12内
では空気Aと粉粒体Cは均一に混合される。また、混合
体流出口14、15にもそれぞれ収縮部14a、15a
が設けられており、空気Aと粉粒体Cの混合体Dは該収
縮部14a、15aから流速の速い(例えば20〜30
m/s)噴流となって移送管17、18内に排出され
る。
The air inlet 13 of the mixing tank 12 is provided with the contraction portion 13a as described above, and the flow rate of the air A in the air pipe 16 (for example, 10 m / s) passes through the contraction portion 13a. Since it is accelerated (for example, 20 to 30 m / s) and flows into the mixing tank 12 as a jet, the air A and the granular material C are uniformly mixed in the mixing tank 12. Also, the contraction portions 14a, 15a are provided at the mixture outlets 14, 15, respectively.
The mixture D of the air A and the granular material C has a high flow rate (for example, 20 to 30) from the contraction portions 14a and 15a.
m / s) and is discharged into the transfer pipes 17 and 18 as a jet.

【0019】上記実施形態例では、混合槽12に混合体
流出口14、15を複数個(図では2個)設け、それぞ
れに移送管17、18を接続して、粉粒体を複数箇所に
移送する場合の例を示したが、粉粒体を1箇所に移送す
る場合は、混合体流出口は1個でよいことは当然であ
る。
In the above-described embodiment, a plurality of (two in the figure) mixture outlets 14 and 15 are provided in the mixing tank 12, and transfer pipes 17 and 18 are connected to each of the outlets 14 and 15, so that the powder and granules can be placed at a plurality of locations. Although an example in which the powder is transferred has been described, it is natural that only one mixture outlet is required when the powder is transferred to one place.

【0020】上記のように本発明に係る粉粒体移送装置
は、粉粒体貯留槽11の下端に混合槽12を配備するこ
とにより、粉粒体貯留槽11から切出された粉粒体は混
合槽12内で空気と均一に混合される。これにより粉粒
体は目詰まりを発生することなく、移送管17、18を
通って移送される。空気流入口13及び混合体流出口1
4、15に断面積の小さい収縮部13a、14a、15
aを設けているので、混合槽12内に流入する空気Aの
流速を速めることができ、この流速の速い空気が混合槽
12内で速い旋回流を発生するから、混合槽12内に流
入した粉粒体Cはこの旋回流により空気と均一に混合
し、粉粒体の移送をスムーズに行なうことができる。
As described above, the powder and granular material transfer device according to the present invention is provided with the mixing tank 12 at the lower end of the powder and particle storage tank 11 so that the powder and granular material cut out from the powder and particle storage tank 11 is provided. Is uniformly mixed with air in the mixing tank 12. As a result, the granular material is transferred through the transfer pipes 17 and 18 without causing clogging. Air inlet 13 and mixture outlet 1
The contraction portions 13a, 14a, and 15 having small cross-sectional areas
a, the flow rate of the air A flowing into the mixing tank 12 can be increased, and the air having the high flow velocity generates a fast swirling flow in the mixing tank 12, so that the air A flows into the mixing tank 12. The powder C is uniformly mixed with the air by the swirling flow, so that the powder C can be smoothly transferred.

【0021】図3は本発明に係る粉粒体移送装置を用い
て水処理設備の沈砂池或いは着水井にドライ活性炭を注
入するための装置の構成を示す図である。図3におい
て、図2と同一符号を付した部分は同一又は相当部分を
示す。図3において、20は沈砂池或いは着水井であ
り、該沈砂池或いは着水井20にはドライ活性炭を水中
に注入するための注入機21が配置されている。
FIG. 3 is a view showing the configuration of an apparatus for injecting dry activated carbon into a sand basin or a landing well of a water treatment facility using the granular material transfer apparatus according to the present invention. In FIG. 3, portions denoted by the same reference numerals as those in FIG. 2 indicate the same or corresponding portions. In FIG. 3, reference numeral 20 denotes a sand basin or landing well, in which an injector 21 for injecting dry activated carbon into water is disposed.

【0022】図4は注入機21の構成を示す図であり、
図示するように注入機21はモータMにより回転するシ
ャフト21b、該シャフト21bを取り囲むようにステ
ータチューブ21aが配置されている。該ステータチュ
ーブ21aには吸込口21cが設けられ、該吸込口21
cに本発明に係る粉粒体移送装置の移送管17が接続さ
れる。また、シャフト21bの先端にはロータ22が取
り付けられ、該ロータ22を囲むようにステータ23及
びカバーリング24が設けられている。
FIG. 4 is a view showing the structure of the injector 21.
As shown, the injector 21 has a shaft 21b rotated by a motor M, and a stator tube 21a surrounding the shaft 21b. The stator tube 21a is provided with a suction port 21c.
The transfer pipe 17 of the granular material transfer device according to the present invention is connected to c. A rotor 22 is attached to the tip of the shaft 21b, and a stator 23 and a cover ring 24 are provided so as to surround the rotor 22.

【0023】注入機21のモータMを起動することによ
り、ロータ22が回転し、水がステータ23の上部から
矢印Eに示すように流れ込み、その下端から矢印Fに示
すように流出してステータ23の回りに旋回流を形成す
る。これによりステータチューブ21aを通して移送管
17内に空気吸引力が作用する。この状態で図3のバル
ブ25、26を開くと、空気管16を通って混合槽12
内に空気が流入すると共に、該空気と粉粒体貯留槽11
から粉粒体切出機19で切出されたドライ活性炭が混合
され、移送管17を通して注入機21のステータチュー
ブ21aに送られ、その先端から水中に注入される。
When the motor M of the injector 21 is started, the rotor 22 rotates, and water flows in from the upper portion of the stator 23 as shown by an arrow E, and flows out from the lower end thereof as shown by an arrow F to flow out of the stator 23. Form a swirling flow around. Thereby, an air suction force acts on the transfer pipe 17 through the stator tube 21a. When the valves 25 and 26 in FIG. 3 are opened in this state, the mixing tank 12 is passed through the air pipe 16.
When the air flows into the inside, the air and the granular material storage tank 11
, Dry activated carbon cut out by the powder and grain extractor 19 is mixed, sent to the stator tube 21a of the injector 21 through the transfer pipe 17, and injected into water from the tip.

【0024】図5は本発明に係る粉粒体移送装置を用い
る水処理設備の一例を示す図である。図5において、3
2は取水施設であり、該取水施設32で取水された水は
着水井に流入する。該着水井33には図4に示すような
構成の粉粒状の活性炭を注入する活性炭注入機34が設
けられている。31は図2に示すような構成の粉粒体移
送装置であり、粉粒状の活性炭を活性炭注入機34に移
送するようになっている。活性炭注入機34により着水
井33の水中に活性炭が注入され、該活性炭が注入され
た水は混和池35に流入し、該混和池35からフロック
形成池36、薬品沈殿池37、急速濾過池38、浄水池
39を通って処理水41となり、配水池40を通って配
水される。
FIG. 5 is a diagram showing an example of a water treatment facility using the granular material transfer device according to the present invention. In FIG. 5, 3
Reference numeral 2 denotes a water intake facility, and water taken in the water intake facility 32 flows into a landing well. The landing well 33 is provided with an activated carbon injector 34 for injecting powdered and granular activated carbon having a configuration as shown in FIG. Reference numeral 31 denotes a granular material transfer device having a configuration as shown in FIG. 2, which transfers granular active carbon to an activated carbon injector 34. Activated carbon is injected into the water of the landing well 33 by the activated carbon injecting machine 34, and the water into which the activated carbon is injected flows into the mixing pond 35, and from the mixing pond 35, a floc forming pond 36, a chemical sedimentation pond 37, and a rapid filtration pond 38. The treated water 41 passes through the water purification reservoir 39 and is distributed through the water distribution reservoir 40.

【0025】上記のように着水井33に設けた活性炭注
入機34の粉粒状活性炭を移送する粉粒体移送装置に図
2に示すような構成の粉粒体移送装置を用いることによ
り、粉粒状の活性炭を目詰まり等を発生させることなく
スムーズに効率よく移送できるから、水処理設備を効率
良く連続運転でき、水処理効率を大幅に向上させること
ができる。
As described above, by using the granular material transfer device having the structure shown in FIG. 2 as the granular material transfer device for transferring the granular active carbon of the activated carbon injecting machine 34 provided in the landing well 33, The activated carbon can be smoothly and efficiently transferred without causing clogging or the like, so that the water treatment equipment can be continuously operated efficiently and the water treatment efficiency can be greatly improved.

【0026】なお、本発明の粉粒体移送装置は、水処理
における活性炭、消石灰、乾燥汚泥等の粉粒体移送装置
に限定されるものではない。即ち、粉粒体、例えば砂
糖、食塩、小麦等の粉粒状の食品や薬品を所定の場所か
ら所定の場所に移送する場合に広く利用できる。
It should be noted that the powder / particle transfer apparatus of the present invention is not limited to a powder / particle transfer apparatus for activated carbon, slaked lime, dried sludge and the like in water treatment. That is, the present invention can be widely used for transferring powdery or granular foods or chemicals such as sugar, salt, wheat, etc. from a predetermined place to a predetermined place.

【0027】[0027]

【発明の効果】以上説明したように各請求項に記載の発
明によれば下記のような優れた効果が得られる。
As described above, according to the invention described in each claim, the following excellent effects can be obtained.

【0028】請求項1に記載の発明によれば、粉粒体貯
留槽の下端に混合槽を配備することにより、粉粒体貯留
槽から切出された粉粒体は該混合槽内で空気と均一に混
合されるから、粉粒体を目詰まりを発生させることな
く、移送管を通してスムーズに目的場所に移送すること
ができる。
According to the first aspect of the present invention, by disposing the mixing tank at the lower end of the granular material storage tank, the granular material cut out from the granular material storage tank is subjected to air in the mixing tank. Therefore, the powder can be smoothly transferred to the destination through the transfer pipe without causing clogging.

【0029】請求項2に記載の発明によれば、空気流入
口及び混合体流出口に収縮部を設けたことにより、混合
槽内に流入する空気の流速を速めることができ、この流
速の速い空気が混合槽内で速い旋回流を発生し、混合槽
内に流入した粉粒体はこの旋回流により空気と均一に混
合し、混合体は混合体流出口の収縮部を通って高速で粉
粒体移送管内に噴出されるから、粉粒体を目詰まりを発
生することなく移送することができる。
According to the second aspect of the present invention, the flow rate of the air flowing into the mixing tank can be increased by providing the shrinking portions at the air inlet and the mixture outlet. The air generates a fast swirling flow in the mixing tank, and the powder particles flowing into the mixing tank are uniformly mixed with the air by the swirling flow. Since the particles are ejected into the particle transfer tube, the particles can be transferred without causing clogging.

【0030】請求項3に記載の発明によれば、混合槽に
複数個の混合体流出口を設け、該混合体流出口のそれぞ
れに粉粒体移送管を接続するので、複数の目的場所に粉
粒体を移送することができる。
According to the third aspect of the present invention, a plurality of mixture outlets are provided in the mixing tank, and a powder transfer pipe is connected to each of the mixture outlets. Granules can be transferred.

【0031】請求項4に記載の発明によれば、請求項1
乃至3のいずれか1項に記載の粉粒体移送装置を水処理
設備に利用することにより、効率よく活性炭、消石灰、
乾燥汚泥等の粉粒体を所定の場所から所定の場所に移送
することができ、水処理の効率を向上させることができ
る。
According to the fourth aspect of the present invention, the first aspect is provided.
The activated carbon, slaked lime, and the like are efficiently used by using the granular material transfer device according to any one of (1) to (3) in a water treatment facility.
Granules such as dry sludge can be transferred from a predetermined location to a predetermined location, and the efficiency of water treatment can be improved.

【図面の簡単な説明】[Brief description of the drawings]

【図1】従来の粉粒体移送装置の概略構成を示す図であ
る。
FIG. 1 is a diagram showing a schematic configuration of a conventional granular material transfer device.

【図2】本発明に係る粉粒体移送装置の概略構成を示す
図である。
FIG. 2 is a diagram showing a schematic configuration of a granular material transfer device according to the present invention.

【図3】本発明に係る粉粒体移送装置を用いて水処理設
備の沈砂池或いは着水井にドライ活性炭を注入するため
の装置の構成例を示す図である。
FIG. 3 is a diagram showing a configuration example of an apparatus for injecting dry activated carbon into a sand basin or a landing well of a water treatment facility using the granular material transfer apparatus according to the present invention.

【図4】ドライ活性炭を水中に注入する注入機の構成を
示す図である。
FIG. 4 is a diagram showing a configuration of an injector for injecting dry activated carbon into water.

【図5】本発明に係る粉粒体移送装置を水処理設備の一
例を示す図である。
FIG. 5 is a view showing an example of a water treatment facility using the granular material transfer device according to the present invention.

【符号の説明】[Explanation of symbols]

11 粉粒体貯留槽 12 混合槽 13 空気流入口 14 混合体流出口 15 混合体流出口 16 空気管 17 移送管 18 移送管 19 粉粒体切出機 20 沈砂池或いは着水井 21 注入機 22 ロータ 23 ステータ 24 カバーリング 25 バルブ 26 バルブ 31 粉粒体移送装置 32 取水施設 33 着水井 34 活性炭注入機 35 混和池 36 フロック形成池 37 薬品沈殿池 38 急速濾過池 39 浄水池 40 配水池 41 処理水 DESCRIPTION OF SYMBOLS 11 Granule storage tank 12 Mixing tank 13 Air inlet 14 Mixer outlet 15 Mixer outlet 16 Air pipe 17 Transfer pipe 18 Transfer pipe 19 Granule extractor 20 Sand basin or landing well 21 Injector 22 Rotor 23 Stator 24 Covering 25 Valve 26 Valve 31 Granular material transfer device 32 Water intake facility 33 Landing well 34 Activated carbon injector 35 Mixing pond 36 Floc formation pond 37 Chemical sedimentation pond 38 Rapid filtration pond 39 Purification pond 40 Distribution pond 41 Treated water

───────────────────────────────────────────────────── フロントページの続き (72)発明者 鈴木 隆洋 東京都大田区羽田旭町11番1号 株式会社 荏原製作所内 (72)発明者 松延 紀至 東京都大田区羽田旭町11番1号 株式会社 荏原製作所内 (72)発明者 本橋 寛 東京都大田区羽田旭町11番1号 株式会社 荏原製作所内 (72)発明者 高嶋 洋介 東京都大田区羽田旭町11番1号 株式会社 荏原製作所内 Fターム(参考) 3F047 AA03  ──────────────────────────────────────────────────続 き Continued on the front page (72) Inventor Takahiro Suzuki 11-1 Haneda Asahimachi, Ota-ku, Tokyo Inside Ebara Works Co., Ltd. (72) Inventor Noriyoshi Matsunobu 11-1 Haneda Asahi-cho, Ota-ku, Tokyo Shares (72) Inventor Hiroshi Motohashi 11-1 Haneda Asahimachi, Ota-ku, Tokyo Inside the Ebara Corporation (72) Inventor Yosuke Takashima 11-1 Haneda Asahi-cho, Ota-ku, Tokyo Inside the Ebara Corporation F term (reference) 3F047 AA03

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 粉粒体を貯留する粉粒体貯留槽、該粉粒
体貯留槽の下部に配置した移送管を具備し、粉粒体貯留
槽から切出機で切出した粉粒体を該移送管で空気により
加圧方式或いは吸引方式にて移送する粉粒体移送装置に
おいて、 前記粉粒体貯留槽の下端に空気流入口、混合体流出口を
有する混合槽を配備し、該混合槽で粉粒体貯留槽から切
出された粉粒体と空気流入口から流入した空気とを混合
し、 混合体流出口から前記移送管を通して空気と混合した粉
粒体を所定の場所に移送することを特徴とする粉粒体移
送装置。
1. A powder and granule storage tank for storing powder and granules, and a transfer pipe disposed at a lower portion of the powder and granule storage tank, wherein the powder and granules cut out from the powder and granule storage tank by a cutting machine are provided. In a powder and granular material transfer device for transferring by a pressurized method or a suction method by air through the transfer pipe, a mixing tank having an air inlet and a mixture outlet at a lower end of the powder and particle storage tank is provided, and the mixing is performed. In the tank, the granules cut out from the granule storage tank are mixed with the air flowing from the air inlet, and the granules mixed with the air are transferred from the mixture outlet to the predetermined place through the transfer pipe. A granular material transfer device characterized by performing.
【請求項2】 請求項1に記載の粉粒体移送装置におい
て、 前記空気流入口及び前記混合体流出口に断面積の小さい
収縮部を設けたことを特徴とする粉粒体移送装置。
2. The granular material transfer device according to claim 1, wherein a contraction portion having a small cross-sectional area is provided at the air inlet and the mixture outlet.
【請求項3】 請求項1又は2に記載の粉粒体移送装置
において、 前記混合槽には複数個の混合体流出口が設けられ、該複
数の混合体流出口のそれぞれに移送管を接続したことを
特徴とする粉粒体移送装置。
3. The granular material transfer device according to claim 1, wherein the mixing tank is provided with a plurality of mixture outlets, and a transfer pipe is connected to each of the plurality of mixture outlets. A granular material transfer device, characterized in that:
【請求項4】 粉粒体を所定の場所から所定の場所へ移
送する粉粒体移送装置を具備する水処理設備において、 前記粉粒体移送装置に請求項1乃至3のいずれか1項に
記載の粉粒体移送装置を用いることを特徴とする水処理
設備。
4. A water treatment facility comprising a granular material transfer device for transferring a granular material from a predetermined place to a predetermined place, wherein the granular material transfer device is configured as described in any one of claims 1 to 3. A water treatment facility, characterized by using the granular material transfer device described in the above.
JP31527099A 1999-11-05 1999-11-05 Granular material transfer device and water treatment equipment using the granular material transfer device Expired - Lifetime JP3420140B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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JP3420140B2 JP3420140B2 (en) 2003-06-23

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Country Link
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004130281A (en) * 2002-10-15 2004-04-30 Fuji Photo Film Co Ltd Method and device for submerged powder-addition
JP2021003668A (en) * 2019-06-26 2021-01-14 株式会社イズミフードマシナリ Edible powder melting system

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4728749B2 (en) * 2005-09-09 2011-07-20 水ing株式会社 Powder injection device, powder transfer device, water treatment facility

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004130281A (en) * 2002-10-15 2004-04-30 Fuji Photo Film Co Ltd Method and device for submerged powder-addition
JP2021003668A (en) * 2019-06-26 2021-01-14 株式会社イズミフードマシナリ Edible powder melting system
JP7373311B2 (en) 2019-06-26 2023-11-02 株式会社イズミフードマシナリ Edible powder dissolution system

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