JPH0331116A - Subsidiary air feed method for pneumatic granule transport pipe - Google Patents

Subsidiary air feed method for pneumatic granule transport pipe

Info

Publication number
JPH0331116A
JPH0331116A JP16487089A JP16487089A JPH0331116A JP H0331116 A JPH0331116 A JP H0331116A JP 16487089 A JP16487089 A JP 16487089A JP 16487089 A JP16487089 A JP 16487089A JP H0331116 A JPH0331116 A JP H0331116A
Authority
JP
Japan
Prior art keywords
air
transport pipe
powder
auxiliary air
pipe
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.)
Pending
Application number
JP16487089A
Other languages
Japanese (ja)
Inventor
Tadao Nakahara
中原 忠男
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.)
Chichibu Engineering KK
Original Assignee
Chichibu Engineering KK
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 Chichibu Engineering KK filed Critical Chichibu Engineering KK
Priority to JP16487089A priority Critical patent/JPH0331116A/en
Publication of JPH0331116A publication Critical patent/JPH0331116A/en
Pending legal-status Critical Current

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  • Air Transport Of Granular Materials (AREA)

Abstract

PURPOSE:To improve transport efficiency by injecting subsidiary air supplied on the way of a pneumatic transport pipe for granule so as to be a swirling flow with swirling blades. CONSTITUTION:When subsidiary air is introduced from a subsidiary air feeding pipe 8 against granule moving in a pneumatic transport pipe 5, the subsidiary air is blown out guided with an air introducing part 9 through an air chamber 7 and swirling blades 12. As the subsidiary air is blown out in state of a swirling flown on this way, mixing of goods to be transported and air is improved, force feed capacity is enlarged, and efficient transport is attained.

Description

【発明の詳細な説明】 [発明の目的] (産業上の利用分野) 本発明は、粉粒体を輸送管を用いて空気輸送する場合の
粉粒体輸送管の補助空気給気方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Object of the Invention] (Industrial Field of Application) The present invention relates to a method for supplying auxiliary air to a powder or granular material transport pipe when the powder or granular material is pneumatically transported using the transport pipe.

(従来の技術) 粉粒体、例えばセメント等はバラ輸送が行なわれる。第
3図に示されるように、タンク車1にて輸送されてきた
セメントは、輸送管2を経由してセメントサイロ3へ空
気輸送することが行なわれる。この場合の空気輸送とは
、圧縮した空気と共に粉粒体を圧送する方式である。し
かし輸送されるものが粉粒体であるため輸送管の閉塞を
防止する必要があり、そのため輸送管の中間所定位置に
補助空気供給部(以下ブースターと称す)を設けて、効
率的な輸送をはかつている。
(Prior Art) Powdered materials, such as cement, are transported in bulk. As shown in FIG. 3, cement transported by a tank car 1 is pneumatically transported to a cement silo 3 via a transport pipe 2. The pneumatic transport in this case is a method of pumping the powder together with compressed air. However, since the material to be transported is powder or granular material, it is necessary to prevent clogging of the transport pipe. Therefore, an auxiliary air supply section (hereinafter referred to as a booster) is installed at a predetermined position in the middle of the transport pipe to ensure efficient transport. It's getting older.

(発明が解決しようとする課題) 上記従来方式によれば、圧縮空気の押し出し圧及びブー
スターによってとりあえずは輸送管の閉塞防止は達成で
きる。しかし輸送管内の水平管部や斜め管部等ては、堆
積物が発生しやすく、効率的な空気輸送システムの出現
が望まれていた。
(Problems to be Solved by the Invention) According to the above-mentioned conventional system, prevention of clogging of the transport pipe can be achieved for the time being by the extrusion pressure of compressed air and the booster. However, deposits are likely to be generated in horizontal pipe sections and diagonal pipe sections within transport pipes, so there has been a desire for an efficient pneumatic transport system.

本発明は上記事情に鑑みてなされたものであり、粉粒体
の効率的な空気輸送の可能な粉粒体空気輸送管の補助空
気給気方法を提供することを目的としている。
The present invention has been made in view of the above circumstances, and it is an object of the present invention to provide a method for supplying auxiliary air to a powder air transport pipe, which allows efficient pneumatic transportation of powder and granules.

[発明の構成] (課題を解決するための手段) 上記目的を達成するため、本発明では粉粒体空気輸送管
本体(以下空気輸送管と称す)に対して補助空気を供給
して粉粒体を輸送する補助空気供給方法において、補助
空気は旋回羽根を介して旋回流として噴出させるように
した。
[Structure of the Invention] (Means for Solving the Problems) In order to achieve the above object, the present invention supplies auxiliary air to a powder air transport pipe body (hereinafter referred to as an air transport pipe) to transport powder particles. In the auxiliary air supply method for transporting a body, auxiliary air is jetted out as a swirling flow through swirling vanes.

(作 用) したがって空気輸送管内の輸送物に対して補助空気が旋
回流として噴出させることにより、空気との混合が十分
良く行なわれ、輸送管内への付着や沈降が防止でき、効
率的な輸送が可能となる。
(Function) Therefore, by ejecting the auxiliary air as a swirling flow to the transported objects in the air transport pipe, it is sufficiently mixed with air, and adhesion and sedimentation inside the transport pipe can be prevented, resulting in efficient transport. becomes possible.

(実施例) 以下図面を参照して実施例を説明する。(Example) Examples will be described below with reference to the drawings.

第1図は本発明よる空気輸送管の補助空気給気方法を説
明するための一実施例の構成図である。
FIG. 1 is a block diagram of an embodiment for explaining the method for supplying auxiliary air to an air transport pipe according to the present invention.

そして第2図は一部切欠して示した斜視図である。FIG. 2 is a partially cutaway perspective view.

第1図及び第2図において、4はブースターてあり、こ
の種の構成のものを空気輸送管の中間部分又は曲管の入
口部分等に取付けて使用する。
In FIGS. 1 and 2, reference numeral 4 denotes a booster, and a booster having this type of structure is used by being attached to the middle part of an air transport pipe or the entrance part of a curved pipe.

以下、ブースターの構成を説明する。ブースター1は空
気輸送管5と、この空気輸送管5と同心円状に被覆した
異径管6とがらなり、その間にエアーチャンバー7が設
けられる。8は異径管6に設けた補助空気給気管で、内
部にはエアー導入路9が空気輸送管5の周囲に設けられ
、この傾斜に合せて補助空気給気管8も取付けられる。
The configuration of the booster will be explained below. The booster 1 consists of an air transport pipe 5 and a different diameter pipe 6 concentrically covered with the air transport pipe 5, with an air chamber 7 provided therebetween. Reference numeral 8 denotes an auxiliary air supply pipe provided on the pipe 6 of different diameters, and an air introduction passage 9 is provided inside the air transport pipe 5 around the air transport pipe 5, and an auxiliary air supply pipe 8 is also attached to match this inclination.

なおエアー導入路9は空気輸送管5の外周に螺旋状に取
付けである。エアーチャンバー7の一端は盲板1゜にて
閉塞され、他端の出口側11は開放とし、がつエアーチ
ャンバーの噴出部の周りには旋回羽根12が設けられる
Note that the air introduction path 9 is spirally attached to the outer periphery of the air transport pipe 5. One end of the air chamber 7 is closed by a blind plate 1°, the other end, the outlet side 11, is open, and a swirling vane 12 is provided around the ejection part of the air chamber.

以上の構成をもとに作用説明をする。The operation will be explained based on the above configuration.

前記した通り、ブースター4は空気輸送管の中間所定位
置に取付けられ、空気輸送管5内を右方向から左方向へ
向けて実線矢印に従って粉粒体を輸送している。
As described above, the booster 4 is attached to a predetermined position in the middle of the air transport pipe, and transports the powder from the right to the left in the air transport pipe 5 according to the solid arrow.

この際、補助空気給気管8からは補助空気がエアー導入
路9をガイドとして取込まれ、エアーチャンバー7内を
経由し旋回羽根12を介して空気輸送管5内に噴出させ
る。勿論、旋回羽根12は9のガイド角度方向に合せて
取付けであるため、噴出エアーの旋回流を助長させる。
At this time, auxiliary air is taken in from the auxiliary air supply pipe 8 using the air introduction path 9 as a guide, passes through the air chamber 7, and is ejected into the air transport pipe 5 via the swirl vane 12. Of course, since the swirling vanes 12 are attached in accordance with the guide angle direction 9, the swirling flow of the ejected air is promoted.

上記した補助空気の量は空気輸送管(本管)の空気量の
10%〜50%でよく、更に補助空気を空気輸送管(本
管)と別個の空気源より給気する場合は、空気輸送管の
圧力センサーにより給気量を調整して、経済的な空気使
用量とすればよい。
The amount of auxiliary air mentioned above may be 10% to 50% of the air amount of the air transport pipe (main pipe), and if the auxiliary air is supplied from an air source separate from the air transport pipe (main pipe), The amount of air supplied can be adjusted using a pressure sensor in the transport pipe to achieve an economical amount of air usage.

[発明の効果] 以上説明したように、本発明によれば補助エアーを旋回
流として噴出させるようにしたので、以下に列挙する効
果を奏する。
[Effects of the Invention] As explained above, according to the present invention, the auxiliary air is ejected as a swirling flow, so that the following effects are achieved.

(イ)輸送物とエアーとの混合性が一層良くなり、空気
輸送管内への粉粒体の付着や沈降を防止できる。
(a) The mixability of the transported material and air is further improved, and it is possible to prevent the adhesion and sedimentation of particulate matter inside the air transport pipe.

(ロ)輸送物とエアーとの混合性を高めることにより、
圧送能力が向上すると共に、数種の材料物を圧送する場
合の混合性が向上する。
(b) By increasing the mixability of transported objects and air,
The pumping capacity is improved and the mixability when pumping several types of materials is improved.

(ハ)空気輸送管内の圧力損失に応じて給気量を調整す
ることができるため、経済的な空気使用量となり、動力
低減が図られる。
(c) Since the amount of air supply can be adjusted according to the pressure loss within the air transport pipe, the amount of air used is economical and the power consumption can be reduced.

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

第1図は本発明による空気輸送管の補助エアー給気方法
を説明するための一実施例の構成図、第2図は一部切欠
して示した斜視図、第3図はセメントのバラ輸送を説明
する図である。
Fig. 1 is a configuration diagram of an embodiment for explaining the auxiliary air supply method for an air transport pipe according to the present invention, Fig. 2 is a partially cutaway perspective view, and Fig. 3 is a transportation of cement in bulk. FIG.

Claims (3)

【特許請求の範囲】[Claims] (1)粉粒体−空気輸送管の中間に補助空気を供給して
粉粒体を輸送する補助空気給気方法において、前記補助
空気は旋回羽根を介して旋回流として噴出させることを
特徴とする粉粒体空気輸送管の補助空気給気方法。
(1) An auxiliary air supply method for transporting granular materials by supplying auxiliary air to the middle of a granular material-air transport pipe, characterized in that the auxiliary air is ejected as a swirling flow through swirling vanes. Supplementary air supply method for powder and granular air transport pipes.
(2)補助空気は、粉粒体空気輸送管に対して同心円状
に取付けた空気チャンバー内に、螺旋状ガイドを介して
取込むことを特徴とする請求項1項記載の粉粒体空気輸
送管の補助空気給気方法。
(2) The auxiliary air is taken in through a spiral guide into an air chamber installed concentrically with respect to the powder and granule air transport pipe. Auxiliary air supply method for pipes.
(3)補助空気は、粉粒体空気輸送管内の輸送速度及び
圧力センサーにより給気量を調整して送出することを特
徴とする請求項1項記載の粉粒体空気輸送管の補助空気
給気方法。
(3) The auxiliary air supply for the powder and granular material air transport pipe according to claim 1, characterized in that the auxiliary air is sent out after adjusting the amount of air supplied by a transport speed and pressure sensor in the powder and granular material air transport pipe. How to care.
JP16487089A 1989-06-27 1989-06-27 Subsidiary air feed method for pneumatic granule transport pipe Pending JPH0331116A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16487089A JPH0331116A (en) 1989-06-27 1989-06-27 Subsidiary air feed method for pneumatic granule transport pipe

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16487089A JPH0331116A (en) 1989-06-27 1989-06-27 Subsidiary air feed method for pneumatic granule transport pipe

Publications (1)

Publication Number Publication Date
JPH0331116A true JPH0331116A (en) 1991-02-08

Family

ID=15801492

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16487089A Pending JPH0331116A (en) 1989-06-27 1989-06-27 Subsidiary air feed method for pneumatic granule transport pipe

Country Status (1)

Country Link
JP (1) JPH0331116A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5498360A (en) * 1993-06-30 1996-03-12 Nomura Kohsan Co., Ltd. Process for recycling used-up dry cells, and ferrite production process
WO2011069588A1 (en) * 2009-12-09 2011-06-16 Uhde Gmbh Device for feeding a fluid into a solid-conveying line
CN105731080A (en) * 2016-04-07 2016-07-06 河南理工大学 Bi-directionally adjusted multipurpose vortex flow swirler
JP2017007841A (en) * 2015-06-24 2017-01-12 春日電機株式会社 Charging device for particulate matter
CN109436807A (en) * 2018-12-11 2019-03-08 马鞍山意泰诺环保科技有限公司 Horizontal fluidised device for low-pressure pneumatic conveying

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5498360A (en) * 1993-06-30 1996-03-12 Nomura Kohsan Co., Ltd. Process for recycling used-up dry cells, and ferrite production process
WO2011069588A1 (en) * 2009-12-09 2011-06-16 Uhde Gmbh Device for feeding a fluid into a solid-conveying line
CN102712426A (en) * 2009-12-09 2012-10-03 蒂森克虏伯伍德有限公司 Device for feeding a fluid into a solid-conveying line
JP2013513535A (en) * 2009-12-09 2013-04-22 ティッセンクルップ・ウーデ・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツング Apparatus for supplying fluid into a solids transfer conduit
AU2010330410B2 (en) * 2009-12-09 2014-07-24 Thyssenkrupp Uhde Gmbh Device for feeding a fluid into a solid-conveying line
JP2017007841A (en) * 2015-06-24 2017-01-12 春日電機株式会社 Charging device for particulate matter
CN105731080A (en) * 2016-04-07 2016-07-06 河南理工大学 Bi-directionally adjusted multipurpose vortex flow swirler
CN109436807A (en) * 2018-12-11 2019-03-08 马鞍山意泰诺环保科技有限公司 Horizontal fluidised device for low-pressure pneumatic conveying

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