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JPH0134900B2 - - Google Patents
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JPH0134900B2 - - Google Patents

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Publication number
JPH0134900B2
JPH0134900B2 JP55099686A JP9968680A JPH0134900B2 JP H0134900 B2 JPH0134900 B2 JP H0134900B2 JP 55099686 A JP55099686 A JP 55099686A JP 9968680 A JP9968680 A JP 9968680A JP H0134900 B2 JPH0134900 B2 JP H0134900B2
Authority
JP
Japan
Prior art keywords
flow rate
air
powder
flow
air volume
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
JP55099686A
Other languages
Japanese (ja)
Other versions
JPS5727831A (en
Inventor
Toshio Maruo
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.)
Nisshin Seifun Group Inc
Original Assignee
Nisshin Seifun Group Inc
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 Nisshin Seifun Group Inc filed Critical Nisshin Seifun Group Inc
Priority to JP9968680A priority Critical patent/JPS5727831A/en
Priority to US06/285,280 priority patent/US4402635A/en
Priority to DE3128807A priority patent/DE3128807C2/en
Priority to GB8122487A priority patent/GB2080234B/en
Publication of JPS5727831A publication Critical patent/JPS5727831A/en
Publication of JPH0134900B2 publication Critical patent/JPH0134900B2/ja
Granted legal-status Critical Current

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  • Air Transport Of Granular Materials (AREA)

Description

【発明の詳細な説明】 本発明は多管式空気輸送系において各管の所定
箇所に定風量調節装置を設けた集合管空気輸送系
に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a multi-tube pneumatic transport system in which a constant air volume adjusting device is provided at a predetermined location of each pipe in the multi-pipe pneumatic transport system.

従来の多管式空気輸送系は後に詳述するが、第
1図に線図的に示すようなものである。このよう
な系では当初ダンパにより各枝管を流れる風量を
所定の値に設定してその状態で運転を続行する。
しかし、現実に各枝管を流れる輸送物の量は大き
く変化し、その影響により各枝管を流れる風量も
変化する。そこでこの所定風量値の設定に際して
は、各枝管内で発生し得ると考えられる粉粒体の
最大混合比においても粉粒体を空気輸送し得る風
速を得るための風量を経験的に求め、設定してい
る。従つて、この設定風量は全枝管の混合比が一
定な定常運転時のみを考えた場合のそれに比して
相当過大なものとなつている。従つて、各枝管に
おける実混合比は通常最大混合比より相当小さ
く、過大な風量が無駄に流れ、また空気動力の消
費増大、ダクトの摩耗を来す結果になつている。
このため、空気源のモータおよびブロワは過大な
容量のものを必要とするから、設備費もさること
ながら、運転は実に不経済な状態でなされてい
る。また、ある枝管に過大な風量が流れると、他
の枝管の風量は減少し、この場合の混合比によつ
ては管中に粉粒体の停滞、最悪の場合には閉塞を
起すという障害をも生ずる。このように、従来の
空気輸送系は設計値を過大にすることがあり、ま
たトラブルが多いという欠点がある。
A conventional multi-tube pneumatic conveyance system will be described in detail later, and is diagrammatically shown in FIG. In such a system, the damper initially sets the amount of air flowing through each branch pipe to a predetermined value and continues operation in that state.
However, in reality, the amount of cargo flowing through each branch pipe varies greatly, and the amount of air flowing through each branch pipe also changes due to this influence. Therefore, when setting this predetermined air volume value, we empirically determined and set the air volume to obtain a wind speed that can air transport the powder and granular material even at the maximum mixing ratio of the powder and granular material that is considered to occur in each branch pipe. are doing. Therefore, this set air volume is considerably larger than that when considering only steady operation in which the mixing ratio of all branch pipes is constant. Therefore, the actual mixing ratio in each branch pipe is usually much lower than the maximum mixing ratio, resulting in an excessive amount of air flowing wastefully, increased consumption of air power, and wear of the duct.
For this reason, the air source motor and blower require an excessively large capacity, which not only increases equipment costs but also makes the operation extremely uneconomical. In addition, if an excessive amount of air flows through one branch pipe, the air volume in other branch pipes decreases, and depending on the mixing ratio in this case, powder and granules may stagnate in the pipe, or in the worst case, cause blockage. It also causes problems. As described above, the conventional pneumatic transportation system has the disadvantage that the design value may be excessively large and there are many troubles.

従つて、本発明の目的は各枝管に流す風量を一
定値に保持し、安定した運転がなされる空気輸送
系を提供しようとするにある。
Therefore, an object of the present invention is to provide an air transport system that maintains the amount of air flowing through each branch pipe at a constant value and operates stably.

さらに、本発明の他の目的は空気輸送するため
の設備および運転コストの低減化を図ろうとする
にある。
Furthermore, another object of the present invention is to reduce equipment and operating costs for pneumatic transportation.

本発明によれば、空気輸送系を構成する各枝管
系の一部に混合比の変化等による圧力変動に対応
できる定風量調節装置を設け、各枝管系の混合比
が増減しても常に一定の所定風量が維持されるよ
う構成する。即ち、本発明は、主管に連通する多
数の枝管に空気を流して粉粒体を輸送する系にお
いて、 各枝管の所定個所に、絞り部を有するベンチユ
リ型ハウジングと、該ハウジング内の前記絞り部
付近に設置され、ハウジング軸方向に移動可能な
流量調整部材と、該流量調整部材を空気流の上流
方向へ付勢する付勢手段、前記粉粒体の輸送量に
応じて流量調整基準値を調整するため、前記流量
調整部材の基準位置を設定するための手動調節手
段とを有し、前記粉粒体の輸送量に応じて前記調
節手段により設定された基準位置から、空気流の
流速に応じて前記流量調整部材が自動的に移動
し、流路の横断面積を増減することにより流量を
一定の流量調整基準値に調整するよう構成された
定風量調節装置を設け、前記各枝管の流量を所定
比を保つように制御するよう構成したことを特徴
とする空気輸送系を提供するものである。
According to the present invention, a part of each branch pipe system constituting the air transport system is provided with a constant air volume adjustment device that can respond to pressure fluctuations due to changes in the mixing ratio, etc., so that even if the mixing ratio of each branch pipe system increases or decreases, The configuration is such that a constant predetermined air volume is always maintained. That is, the present invention provides a system for transporting powder by flowing air through a large number of branch pipes communicating with a main pipe. a flow rate adjustment member installed near the constriction portion and movable in the axial direction of the housing; a biasing means for biasing the flow rate adjustment member in the upstream direction of the air flow; and a flow rate adjustment standard according to the amount of transported powder and granular material. and a manual adjustment means for setting a reference position of the flow rate adjustment member in order to adjust the value, the air flow is adjusted from the reference position set by the adjustment means according to the amount of powder or granular material transported. A constant air volume adjusting device is provided in which the flow rate adjusting member automatically moves according to the flow velocity to adjust the flow rate to a constant flow rate adjustment reference value by increasing or decreasing the cross-sectional area of the flow path, and each of the branches The present invention provides an air transport system characterized in that it is configured to control the flow rate of the pipes so as to maintain a predetermined ratio.

次に、本発明による空気輸送系を従来のものと
比較しつつ図示の実施例につき説明する。
Next, the illustrated embodiments of the pneumatic transport system according to the present invention will be explained while comparing it with a conventional system.

第1図には従来の空気輸送系を示す。代表的に
吸引式のものについて図示するが、圧送式のもの
にも本発明を適用できるのは勿論のことである。
この系では、主管Lは多数の枝管L1,L2,L3
Loに分岐し、各枝管にはサイクロンC1,C2,C3
…Co、混合器M1,M2,M3…Moが設けられ、ダ
ンパD1,D2,D3…Doにより風量調節が行われ
る。ブロワ1より吸引空気は各枝管内に混合器よ
り粉粒体を適度な混合比で吸引し、サイクロンで
粉粒体を分離し、バツクフイルタ2で除塵されて
排気される。このように粉粒体を空気輸送するに
はある風速(量)が必要であり、これは輸送物の
物性、例えば、粒度、形状、粘着性、吸湿性等や
空気との混合比によつて決定される。また、混合
比は常時変動しており、その変動幅も相当大き
く、混合比が最大になるであろうと考えられる値
について現在ではダンパの開放度、すなわち、輸
送風速を得るための風量Qを決定している。しか
し、通常時は各枝管内の混合比は仮想した最大混
合比より小さく、その分は粉粒体の輸送用空気と
して使用されずに浪費されてしまつている。ま
た、ある枝管、例えば、Loの混合器Moからの粉
粒体の供給量が多くなり、その混合比が高くなつ
た場合、この系の風量は減り、流れ易い他の管系
L1,L2,…Lo-1に分散されて流れる。これらの
管系の分散された風量は抑止されることなく流れ
続け、無駄な風速として浪費される。更に混合比
が増加すると上記現象が加速されて粉粒体の輸送
が不可能となり、終にはこの系Loは閉塞するこ
とすらある。これはLoに流れるべき風量が他の
管系へ容易に流れるようダンパが設定されている
からである。
FIG. 1 shows a conventional pneumatic transport system. Although a suction type is illustrated as a representative example, it goes without saying that the present invention can also be applied to a pressure feeding type.
In this system, the main pipe L has many branch pipes L 1 , L 2 , L 3 . . .
Branched into L o , each branch pipe has cyclones C 1 , C 2 , C 3
...C o , mixers M 1 , M 2 , M 3 ... Mo are provided, and the air volume is adjusted by dampers D 1 , D 2 , D 3 ...D o . The suction air from the blower 1 sucks powder and granules into each branch pipe from a mixer at an appropriate mixing ratio, separates the powder and granules with a cyclone, removes dust with a back filter 2, and exhausts the air. In this way, a certain wind speed (amount) is required to transport powder and granular materials by air, and this depends on the physical properties of the transported material, such as particle size, shape, stickiness, hygroscopicity, etc., and the mixing ratio with air. It is determined. In addition, the mixing ratio is always changing, and the range of fluctuation is quite large, so the damper opening degree, that is, the air volume Q to obtain the transport wind speed, is currently determined based on the value that is considered to be the maximum mixing ratio. are doing. However, under normal conditions, the mixing ratio in each branch pipe is smaller than the imaginary maximum mixing ratio, and this amount is wasted without being used as air for transporting the powder or granules. In addition, if the amount of powder and granules supplied from a certain branch pipe, for example, the mixer M o of L o increases, and the mixing ratio increases, the air volume of this system will decrease, and other pipe systems that are easy to flow will be
It flows dispersed into L 1 , L 2 , ...L o-1 . The dispersed air volume of these pipe systems continues to flow without being restrained and is wasted as wasted wind speed. If the mixing ratio further increases, the above phenomenon will be accelerated, making it impossible to transport the powder and granules, and eventually this system L o may even become clogged. This is because the damper is set so that the amount of air that should flow to Lo can easily flow to other pipe systems.

そこで、本発明においては、各枝管系にダンパ
の代りに緩衝能力を有する定風量調節装置V1
V2,V3…Voを設ける(第2図参照)。この定風
量調節装置としては、第3図に一例を示すような
ものを使用することができる。
Therefore, in the present invention, each branch pipe system is equipped with a constant air volume adjusting device V 1 having a buffering capacity instead of a damper.
V 2 , V 3 ...V o are provided (see Figure 2). As this constant air volume adjusting device, an example as shown in FIG. 3 can be used.

この装置は、絞り部8を有するベンチユリ型ハ
ウジング3を有し、該ハウジング3の絞り部付近
には、流量調整部材であるコーン4がハウジング
3の軸方向、即ち空気の流れ方向に移動可能なよ
うに設置されている。また、コーン4にはばね5
が取り付けられ、空気流の上流方向へ付勢されて
いる。なお、コーン4の基準位置は、粉粒体の輸
送量に応じて、流量調整基準値を調整することが
できるように、手動調節手段6を操作して棒7を
軸方向に移動させることにより調節可能となつて
いる。
This device has a bench lily type housing 3 having a constriction part 8, and near the constriction part of the housing 3, a cone 4, which is a flow rate adjusting member, is movable in the axial direction of the housing 3, that is, in the direction of air flow. It is set up like this. Also, a spring 5 is attached to the cone 4.
is attached and biased in the upstream direction of the airflow. The reference position of the cone 4 is determined by operating the manual adjustment means 6 and moving the rod 7 in the axial direction so that the flow rate adjustment reference value can be adjusted according to the amount of powder and granular material transported. It is adjustable.

ここで、手動調節手段6によるコーン4の基準
位置設定は、初期設定を行つてもよく、粉粒体の
輸送中に設定値の変更を行つてもよい。
Here, the reference position setting of the cone 4 by the manual adjustment means 6 may be performed initially, or the set value may be changed during transportation of the powder or granular material.

このため、輸送する粉粒体の種類、量、形状に
応じて、適当な流量調整基準値を選択することが
できるし、途中でこれらが変つても手動調節手段
6を操作して、流量調整基準値を変更できるの
で、各枝管に常に好適な所定の風量を送ることが
できる。
Therefore, it is possible to select an appropriate flow rate adjustment reference value according to the type, amount, and shape of the powder or granular material to be transported, and even if these values change during the process, the flow rate can be adjusted by operating the manual adjustment means 6. Since the reference value can be changed, a suitable predetermined air volume can always be sent to each branch pipe.

コーン4は、前記流量調整基準値に応じた基準
位置を中心としてハウジング3内の矢印で示すよ
うな空気流の風速が速くなると、すなわち、空気
の風圧が強まると、ばね5が圧縮されて下流方向
(第3図で見て右方)に実線で示すように移動し、
コーン4とハウジング3との隙間を狭くし、即ち
絞り部8における流路の横断面積を減少させて流
れの抵抗を高め、風量を減ずる作用をする。逆
に、ハウジング3内の風速が減じて風圧が弱まる
と、ばね5は伸張してコーン4を上流方向(第3
図で見て左方)に点線で示すように移動させ、ハ
ウジング3との隙間を大きくし、即ち絞り部8に
おける流路の横断面積を増大させて流れの抵抗を
弱め、風量を増大する作用をする。このようにし
て各管系L1,L2,L3…Loにこの定風量調節装置
を設けることにより各管系ともに常に一定の風量
Q′だけが流れるようにすることができる。一定
の風量Q′とは従来空気輸送系の場合の風量Qに
比して本発明者の実験によれば20−30%位小さな
値となつており、このために要するブロアおよび
モータの設計値が小さくなるのはもとより、送風
量も小さくなるため運転費(電力)も大幅に(約
20〜30%)減少することが確認されている。な
お、本発明は、枝管の数が比較的多い系に適用す
るのが好ましく、特に5本以上の枝管を有する系
に適用するのが効果的である。
When the wind speed of the air flow increases as indicated by the arrow in the housing 3 around the reference position corresponding to the flow rate adjustment reference value, that is, when the wind pressure of the air increases, the spring 5 is compressed and the cone 4 is moved downstream. Move in the direction (to the right as seen in Figure 3) as shown by the solid line,
The gap between the cone 4 and the housing 3 is narrowed, that is, the cross-sectional area of the flow path in the throttle section 8 is reduced, thereby increasing the flow resistance and reducing the air volume. Conversely, when the wind speed inside the housing 3 decreases and the wind pressure weakens, the spring 5 expands and moves the cone 4 in the upstream direction (third direction).
(to the left in the figure) as shown by the dotted line, increasing the gap with the housing 3, that is, increasing the cross-sectional area of the flow path in the throttle section 8, weakening the flow resistance, and increasing the air volume. do. By providing this constant air volume adjustment device in each pipe system L 1 , L 2 , L 3 ...L o in this way, each pipe system always maintains a constant air volume.
Only Q' can be made to flow. According to experiments conducted by the present inventor, a constant air volume Q' is a value that is approximately 20-30% smaller than the air volume Q in the case of a conventional pneumatic conveyance system, and the design values of the blower and motor required for this purpose are Not only will the amount of air become smaller, but the amount of air blown will also be smaller, so operating costs (electricity) will also be significantly reduced (approx.
20-30%) has been confirmed to decrease. The present invention is preferably applied to a system having a relatively large number of branch pipes, and is particularly effective to be applied to a system having five or more branch pipes.

このように、従来の空気輸送系では系内で浪費
されていた風量が、本発明においては定風量調節
装置により無駄な風量が回避される。従来系では
ダンパの設定値が仮想最大混合比に基いて決定さ
れていたために異常に大きなものとなつており、
本発明における定風量調節装置のように、空気流
の増速に対する抵抗作用と空気流の減速に対する
増速作用が機能できなかつたのである。従つて、
本発明においては、負荷変動に対処することが可
能となり、しかも定常運転時の定風量値は従来の
仮想最大混合比に基づく設定値に比して大幅に小
さい。このため、前述したように系の空気源に用
いるモータおよびブロアはその容量を小さくで
き、ランニングコスト、特に電力消費は大幅に低
減できる上にダクト系の損耗も小さくなつて系の
メンテナンスコストも低減できる。また、本発明
の空気輸送系をよれば、手動調整手段により、流
量調整基準値を粉粒体輸送の初期でも途中でも前
記粉粒体の種類、量、形状に応じて、適当に選択
または変更できるので、各枝管に常に好適な風量
を送ることができる。
In this way, in the conventional pneumatic transport system, the air volume was wasted within the system, but in the present invention, wasted air volume is avoided by the constant air volume adjustment device. In the conventional system, the damper setting value was determined based on the virtual maximum mixture ratio, so it was abnormally large.
Like the constant air volume adjusting device of the present invention, it was unable to function as a resistance against an increase in airflow speed and an acceleration action against a deceleration of an airflow. Therefore,
In the present invention, it is possible to cope with load fluctuations, and the constant air volume value during steady operation is significantly smaller than the conventional set value based on the virtual maximum mixing ratio. Therefore, as mentioned above, the capacity of the motor and blower used as the system's air source can be reduced, significantly reducing running costs, especially power consumption, and reducing wear and tear on the duct system, reducing system maintenance costs. can. Further, according to the pneumatic transportation system of the present invention, the flow rate adjustment reference value can be appropriately selected or changed by the manual adjustment means depending on the type, amount, and shape of the powder or granular material at the beginning or during the transportation of the powder or granular material. This allows a suitable amount of air to be sent to each branch pipe at all times.

以上のような効果はダンパを用いて風量を所定
値に設定する方式にては実現できなかつたもので
あり、本発明は特に省動力上非常に有効であり、
空気輸送系の低エネルギでの安定的運転の実現を
可能ならしめたものである。
The above-mentioned effects could not be achieved by using a damper to set the air volume to a predetermined value, and the present invention is particularly effective in terms of power saving.
This makes it possible to realize stable operation of the pneumatic transport system with low energy consumption.

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

第1図は従来の空気輸送系統図、第2図は本発
明による空気輸送系統図、第3図は第2図の系に
用いる定風量調節装置の断面図である。 L……主管路、L1…,Lo……枝管路、D……
ダンパ、C……サイクロン、M……粉粒体混合
器、V……定風量調節装置、1……ブロワ、2…
…フイルタ、3……ハウジング、4……コーン、
5……ばね、6……位置調節手段、7……棒、8
……絞り部。
FIG. 1 is a diagram of a conventional pneumatic transportation system, FIG. 2 is a diagram of a pneumatic transportation system according to the present invention, and FIG. 3 is a cross-sectional view of a constant air volume adjusting device used in the system of FIG. L... Main pipeline, L 1 ..., L o ... Branch pipeline, D...
Damper, C...Cyclone, M...Powder mixer, V...Constant air volume adjustment device, 1...Blower, 2...
...filter, 3...housing, 4...cone,
5... Spring, 6... Position adjustment means, 7... Rod, 8
...Aperture section.

Claims (1)

【特許請求の範囲】 1 主管に連通する多数の枝管に空気を流して粉
粒体を輸送する系において、 各枝管の所定個所に、絞り部を有するベンチユ
リ型ハウジングと、該ハウジング内の前記絞り部
付近に設置され、ハウジング軸方向に移動可能な
流量調整部材と、該流量調整部材を空気流の上流
方向へ付勢する付勢手段、前記粉粒体の輸送量に
応じて流量調整基準値を調整するため、前記流量
調整部材の基準位置を設定するための手動調節手
段とを有し、前記粉粒体の輸送量に応じて前記調
節手段により設定された基準位置から、空気流の
流速に応じて前記流量調整部材が自動的に移動
し、流路の横断面積を増減することにより流量を
一定の流量調整基準値に調整するよう構成された
定風量調節装置を設け、前記各枝管の流量を所定
比に保つように制御するよう構成したことを特徴
とする空気輸送系。 2 前記枝管の数は5本以上である特許請求の範
囲第1項に記載の空気輸送系。
[Claims] 1. In a system for transporting powder by flowing air through a number of branch pipes communicating with a main pipe, there is provided a bench lily type housing having a constriction section at a predetermined location of each branch pipe, and a flow rate adjusting member installed near the constriction portion and movable in the axial direction of the housing; a biasing means for biasing the flow rate adjusting member in an upstream direction of the air flow; and a flow rate adjusting member according to the transport amount of the powder and granular material. In order to adjust the reference value, it has a manual adjustment means for setting a reference position of the flow rate adjustment member, and the air flow is adjusted from the reference position set by the adjustment means according to the transport amount of the powder or granular material. A constant air volume adjusting device is provided, the flow rate adjusting member is configured to automatically move according to the flow rate of the flow path, and the flow rate is adjusted to a constant flow rate adjustment reference value by increasing or decreasing the cross-sectional area of the flow path. A pneumatic transport system characterized by being configured to control the flow rate of a branch pipe to maintain a predetermined ratio. 2. The pneumatic transport system according to claim 1, wherein the number of branch pipes is five or more.
JP9968680A 1980-07-21 1980-07-21 Pneumatic transport device Granted JPS5727831A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP9968680A JPS5727831A (en) 1980-07-21 1980-07-21 Pneumatic transport device
US06/285,280 US4402635A (en) 1980-07-21 1981-07-20 Pneumatic conveyor system
DE3128807A DE3128807C2 (en) 1980-07-21 1981-07-21 Pneumatic conveyor system for particulate matter
GB8122487A GB2080234B (en) 1980-07-21 1981-07-21 Pneumatic conveyor system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9968680A JPS5727831A (en) 1980-07-21 1980-07-21 Pneumatic transport device

Publications (2)

Publication Number Publication Date
JPS5727831A JPS5727831A (en) 1982-02-15
JPH0134900B2 true JPH0134900B2 (en) 1989-07-21

Family

ID=14253915

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9968680A Granted JPS5727831A (en) 1980-07-21 1980-07-21 Pneumatic transport device

Country Status (1)

Country Link
JP (1) JPS5727831A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3723587A1 (en) * 1987-07-01 1989-01-19 Buehler Ag Geb PNEUMATIC CONVEYOR SYSTEM, METHOD FOR AIR FLOW CONTROL AND USE OF A FLOATING BODY IN SUCH A SYSTEM
JP5090597B2 (en) * 2001-08-07 2012-12-05 ツカサ工業株式会社 Dust collection unit for milling.

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5347598Y2 (en) * 1971-06-04 1978-11-14

Also Published As

Publication number Publication date
JPS5727831A (en) 1982-02-15

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