JP2019131307A - Air-suction type conveyance device - Google Patents

Air-suction type conveyance device Download PDF

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JP2019131307A
JP2019131307A JP2018012348A JP2018012348A JP2019131307A JP 2019131307 A JP2019131307 A JP 2019131307A JP 2018012348 A JP2018012348 A JP 2018012348A JP 2018012348 A JP2018012348 A JP 2018012348A JP 2019131307 A JP2019131307 A JP 2019131307A
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cylinder
inlet
inlet cylinder
air
suction type
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JP7078976B2 (en
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栄一 成川
Eiichi Narukawa
栄一 成川
敏晴 田中
Toshiharu Tanaka
敏晴 田中
武雄 堀
Takeo Hori
武雄 堀
功次 能島
Koji Nojima
功次 能島
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TAIWA SEIKI KK
Taiwa Seiki Corp
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TAIWA SEIKI KK
Taiwa Seiki Corp
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Abstract

To provide an air-suction type conveyance device capable of easily adjusting an intake amount of secondary air, which foreign matter hardly enters from outside.SOLUTION: The air-suction type conveyance device comprises: a conveyance pipeline through which granules pass; and a granule introduction part connected to an upstream side of the conveyance pipeline. The granule introduction part is provided with a connecting pipe, an inlet cylinder, and an outer cylinder. As to the connecting pipe, its upstream side end portion is directed upward, and its downstream side end portion is connected to the conveyance pipeline. The inlet cylinder formed of a net material is connected to an upstream side of the connecting pipe. The outer cylinder whose inner peripheral surface comes in slide contact with an outer peripheral surface of the inlet cylinder is slidable in a vertical direction.SELECTED DRAWING: Figure 1

Description

本発明は、粒体を空気流に乗せて搬送する空気吸引式搬送装置に関する。   The present invention relates to an air suction type conveying apparatus that conveys particles in an air flow.

米などの粒体を搬送するための装置として、空気吸引式の搬送装置がある。これは、搬送管路を有していて、その下流側から管路内の空気を吸引することで、上流から下流へ向かう空気流を形成し、粒体をこの空気流に乗せて搬送するものである。この際、空気を吸引するだけでは、管路内の空気(一次空気)が減少して空気流が形成できなくなってしまうので、管路内の空気を吸引するとともに、外部から管路内に空気(二次空気)を取り込む必要がある。この際、二次空気の量が少なすぎると、搬送管路の途中で詰まりを生じるおそれがあり、二次空気の量が多すぎると、搬送終端部で粒体が十分に減速できず、割れなどの被害が生じるおそれがある。よって、二次空気の取り込み量を適切な値に調整することが重要である。   As an apparatus for conveying grains such as rice, there is an air suction type conveying apparatus. This has a conveyance pipeline, and by sucking the air in the pipeline from the downstream side, an air flow from upstream to downstream is formed, and the particles are carried on this air flow. It is. At this time, if the air is simply sucked, the air in the pipe line (primary air) is reduced and an air flow cannot be formed. Therefore, the air in the pipe line is sucked and air is introduced into the pipe line from the outside. (Secondary air) needs to be taken in. At this time, if the amount of secondary air is too small, there is a risk of clogging in the middle of the conveyance pipeline.If the amount of secondary air is too large, the particles cannot be sufficiently decelerated at the end of conveyance, and cracking occurs. May cause damage. Therefore, it is important to adjust the intake amount of secondary air to an appropriate value.

従来、このような空気吸引式搬送装置における二次空気を取り込むための構造は、特許文献1に示すようなものであった。すなわち、搬送管路の始端部が上方に向けて開口する外気連通口となっており、この外気連通口に対して搬送物の供給口が上方に離隔して対向しており、外気連通口が供給口より大径となっていて、両者の間の隙間から二次空気が取り込まれるものであった。   Conventionally, a structure for taking in secondary air in such an air suction type conveying apparatus is as shown in Patent Document 1. In other words, the start end of the transfer pipe is an open air communication port that opens upward, and the supply port of the conveyed product is opposed to the open air communication port spaced upward, and the open air communication port is The diameter was larger than the supply port, and secondary air was taken in from the gap between the two.

特開2006−205095号公報JP 2006-205095 A

しかしながら、特許文献1の発明は、二次空気の取り込み量の調整、すなわち外気連通口と供給口の間隔の調整が可能な構造とはなっておらず、設計段階で最適な間隔を定めることも困難である。また、近年では搬送物への異物混入についての問題意識が高まっており、特許文献1の発明のような広い開口部を有する構造は、異物混入のおそれがあるため好ましくないものとされている。   However, the invention of Patent Document 1 does not have a structure capable of adjusting the intake amount of secondary air, that is, adjusting the interval between the outside air communication port and the supply port, and may determine an optimum interval at the design stage. Have difficulty. Further, in recent years, awareness of the problem of foreign matter mixing into a conveyed product has increased, and a structure having a wide opening as in the invention of Patent Document 1 is not preferable because of the possibility of foreign matter mixing.

本発明は、このような事情を鑑みたものであり、二次空気の取り込み量を容易に調整可能であって、外部から異物が混入しにくい空気吸引式搬送装置を提供することを目的とする。   The present invention has been made in view of such circumstances, and an object of the present invention is to provide an air suction type conveyance device that can easily adjust the amount of secondary air taken in and that is unlikely to contain foreign matter from the outside. .

本発明のうち請求項1の発明は、粒体が通過する搬送管路と、該搬送管路の上流側に接続する粒体導入部を備え、該粒体導入部は、連結管と、入口筒と、外筒を備え、前記連結管は、上流側端部が上方を向き、下流側端部が前記搬送管路に接続しており、前記入口筒は、網材からなり前記連結管の上流側に接続しており、前記外筒は、内周面が前記入口筒の外周面に摺接するものであって上下方向に摺動自在であることを特徴とする。なお、網材とは、板の全面にわたって複数の貫通孔を間隔を開けて形成したり、針金などを編んで形成したりすることで、複数の網目(孔の部分)を有する素材である。   The invention according to claim 1 of the present invention includes a conveyance pipe line through which particles pass, and a particle introduction part connected to the upstream side of the conveyance pipe. The particle introduction part includes a connecting pipe, an inlet, A pipe and an outer cylinder, and the connecting pipe has an upstream end facing upward, a downstream end connected to the transport pipe, and the inlet pipe is made of a net material and is connected to the connecting pipe. The outer cylinder is connected to the upstream side, and an inner peripheral surface of the outer cylinder is in sliding contact with an outer peripheral surface of the inlet cylinder, and is slidable in the vertical direction. The mesh material is a material having a plurality of meshes (hole portions) by forming a plurality of through holes at intervals over the entire surface of the plate or by knitting a wire or the like.

本発明のうち請求項2の発明は、前記入口筒は、前記搬送管路より断面の外周が長いことを特徴とする。   The invention according to claim 2 of the present invention is characterized in that the inlet cylinder has a longer outer periphery in cross section than the transport pipe.

本発明のうち請求項3の発明は、前記入口筒の下側に延出筒を設けてあり、該延出筒は、外周面が前記入口筒の外周面と面一であることを特徴とする。   The invention according to claim 3 of the present invention is characterized in that an extension tube is provided below the inlet tube, and the outer surface of the extended tube is flush with the outer peripheral surface of the inlet tube. To do.

本発明のうち請求項4の発明は、前記入口筒又は前記外筒の何れか一方は、他方に当接して前記外筒の移動を規制する規制部を有しており、該規制部は、前記外筒が、その上端が前記入口筒の上端より下側となる所定位置より上側へ移動することを規制するものであることを特徴とする。   According to a fourth aspect of the present invention, either one of the inlet tube or the outer tube has a restricting portion that abuts the other and restricts movement of the outer tube, The outer cylinder restricts the upper end of the outer cylinder from moving upward from a predetermined position below the upper end of the inlet cylinder.

本発明のうち請求項5の発明は、粒体を導入するホッパを備え、該ホッパは、前記入口筒の直上に接続していることを特徴とする。   According to a fifth aspect of the present invention, a hopper for introducing particles is provided, and the hopper is connected directly above the inlet tube.

本発明のうち請求項1の発明によれば、網材からなる入口筒から二次空気を取り込むことが可能であって、入口筒の外周面に摺接する外筒を摺動させて入口筒の外周面の露出面積を変化させることで、二次空気の取り込み量を容易に調整可能である。そして、入口筒の網目よりも大きな異物の混入は、確実に防ぐことができる。また、上から下へ通過する粒体に対して水平方向の全周から二次空気が取り込まれて均一に混ざり合うので、搬送効率が良い。   According to the first aspect of the present invention, the secondary air can be taken in from the inlet cylinder made of a mesh material, and the outer cylinder sliding on the outer peripheral surface of the inlet cylinder is slid to slide the inlet cylinder. By changing the exposed area of the outer peripheral surface, the amount of secondary air taken in can be easily adjusted. In addition, it is possible to reliably prevent foreign matters larger than the mesh of the inlet cylinder. Moreover, since secondary air is taken in from the whole circumference of a horizontal direction with respect to the particle | grains which pass from the top to the bottom, and it mixes uniformly, conveyance efficiency is good.

本発明のうち請求項2の発明によれば、入口筒が搬送管路より断面の外周が長いので、同じ長さの場合と比較して、入口筒の表面積が同じ(=網目の総面積が同じ=二次空気の取り込み量が同じ)場合にその高さを低くできるので、結果として粒体導入部全体を小型化できる。   According to the invention of claim 2 of the present invention, since the outer periphery of the cross section of the inlet cylinder is longer than that of the conveying pipe, the surface area of the inlet cylinder is the same as compared to the case of the same length (= total area of the mesh). When the same = the same amount of secondary air is taken in), the height can be lowered, and as a result, the entire granule introduction part can be reduced in size.

本発明のうち請求項3の発明によれば、入口筒の下側に延出筒を設けてあるので、この延出筒部分に外筒を摺動させることで、入口筒の外周面の全体が露出し、二次空気の取り込み量を最大化できる。   According to the third aspect of the present invention, since the extending cylinder is provided below the inlet cylinder, the entire outer peripheral surface of the inlet cylinder can be obtained by sliding the outer cylinder on the extending cylinder portion. Is exposed and the amount of secondary air taken in can be maximized.

本発明のうち請求項4の発明によれば、規制部により外筒の上端が入口筒の上端よりも下側となり、外筒の上端と入口筒の上端の間部分において入口筒が露出するので、所定の二次空気の取り込み量が確保され、全閉状態にならず、搬送管路内の空気量が極端に不足して搬送不能となることが防がれる。   According to the fourth aspect of the present invention, the upper end of the outer cylinder is positioned below the upper end of the inlet cylinder by the restricting portion, and the inlet cylinder is exposed at a portion between the upper end of the outer cylinder and the upper end of the inlet cylinder. A predetermined secondary air intake amount is ensured, the fully closed state is not achieved, and it is prevented that the amount of air in the conveyance pipeline is extremely short and the conveyance becomes impossible.

本発明のうち請求項5の発明によれば、粒体を導入するホッパと入口筒が直結されているので、搬送の入口部から二次空気が供給され、搬送効率が良い。   According to the invention of claim 5 among the present invention, since the hopper for introducing the particles and the inlet cylinder are directly connected, secondary air is supplied from the inlet portion of the conveyance, and the conveyance efficiency is good.

第一実施形態の粒体導入部を示す。The granule introduction part of 1st embodiment is shown. 外筒による二次空気の取り込み量の調整を示し、(a)は全閉状態、(b)は全開状態である。The adjustment of the amount of secondary air taken in by the outer cylinder is shown. (A) is a fully closed state, and (b) is a fully open state. 空気吸引式搬送装置の全体図である。It is a general view of an air suction type conveying apparatus. (a)は第二実施形態の粒体導入部を示し、(b)は第三実施形態の粒体導入部を示す。(A) shows the granule introduction part of 2nd embodiment, (b) shows the granule introduction part of 3rd embodiment.

以下、本発明の空気吸引式搬送装置の具体的な内容について説明する。本発明は種々の粒体を搬送の対象とすることができるものであるが、ここでは精米された米粒を対象とする場合を示す。この空気吸引式搬送装置の第一実施形態は、図3に示すように、搬送管路1と、粒体導入部2と、ホッパ7と、検視管11と、空気分離減速システム12と、バグフィルタ13と、吸引装置14を備えるものである。そして、空気吸引式搬送装置の上流側には、原料タンク15と精米機16が配置されており、下流側にはロータリバルブ17と製品タンク18が配置されている。   Hereinafter, specific contents of the air suction type conveying apparatus of the present invention will be described. Although this invention can make a various grain object become the object of conveyance, the case where the polished rice grain is made into object here is shown. As shown in FIG. 3, the first embodiment of the air suction type conveying apparatus includes a conveying line 1, a granule introduction unit 2, a hopper 7, a visual inspection tube 11, an air separation / deceleration system 12, a bug, A filter 13 and a suction device 14 are provided. A raw material tank 15 and a rice mill 16 are arranged on the upstream side of the air suction type conveying apparatus, and a rotary valve 17 and a product tank 18 are arranged on the downstream side.

原料タンク15は、上部が円筒形であり、下部が漏斗状で下方に向けて窄まった形状である。上部から原料である玄米を投入して、貯留できるものとなっている。精米機16は、直方体形の筐体を有するものであって、上面に玄米の投入口を有しており、この投入口に原料タンク15の下端部が接続されている。よって、精米機16には投入口から順次玄米が投入され、精米が行われる。また、精米機16は、側面の下部に排出口161を有しており、精米された米粒が順次排出される。   The raw material tank 15 has a cylindrical shape in the upper part and a funnel shape in the lower part and is narrowed downward. The brown rice, which is the raw material, can be put in from the top and stored. The rice milling machine 16 has a rectangular parallelepiped housing, and has a brown rice inlet on the upper surface, and the lower end of the raw material tank 15 is connected to this inlet. Therefore, brown rice is sequentially fed into the rice mill 16 from the slot, and rice milling is performed. Moreover, the rice mill 16 has the discharge port 161 in the lower part of the side surface, and the polished rice grains are sequentially discharged.

ホッパ7は、図1に示すように、漏斗状で下方に向けて窄まった形状であり、その上部が精米機16の排出口161に接続されている。虫などの異物混入を防ぐため、排出口161とホッパ7の間は密閉された構造となっている。また、ホッパ7の下端部には、フランジ71を形成してある。   As shown in FIG. 1, the hopper 7 has a funnel shape and is narrowed downward, and its upper portion is connected to the discharge port 161 of the rice mill 16. In order to prevent foreign matters such as insects from entering, the space between the discharge port 161 and the hopper 7 is sealed. A flange 71 is formed at the lower end of the hopper 7.

粒体導入部2は、図1に示すように、ホッパ7の下部に接続されるものであって、連結管3と、入口筒4と、外筒5と、延出筒6を備える。
連結管3は、後記の入口筒4と搬送管路1を連結するものであり、搬送管路1と同径の断面円形の配管であって、上流側端部が上方を向き、下流側に向けて屈曲し下流側端部が水平方向を向いた形状となっている。連結管3の上流側端部には、上方に向けて漏斗状に広がった漏斗状部31を形成してあり、漏斗状部31の上端の内径面積は、搬送管路1の内径面積の1.5〜2.0倍となっている。
入口筒4は、円筒形の網材、より具体的には、円筒形の金属板の周方向と高さ方向のそれぞれにわたって等間隔で貫通孔を形成したいわゆるパンチングメタルからなるものであって、連結管3の上流側に漏斗状部31を介して接続しており(入口筒4の下端部を漏斗状部31の上端部に溶接して固定してある)、漏斗状部31の上端部と同径なので、すなわち搬送管路1よりも大径であり、よって搬送管路1より断面の外周が長い。入口筒4の高さ(上下方向長さ)は、入口筒4の外径よりも低くなっている。また、入口筒4を構成する網材の網目41(孔の部分)は、搬送される米粒よりも小さいものとなっている。さらに、入口筒4の上端部には、フランジ42を形成してあり、入口筒4のフランジ42にホッパ7のフランジ71を当接させてネジ止めして、ホッパ7を入口筒4の直上に接続してある。この入口筒4から、網目41を通して二次空気が取り込まれるものである。そして、入口筒4の下側には、延出筒6を設けてある。
延出筒6は、入口筒4の下端部の漏斗状部31に接続された部分から、さらに下側に向けて延出する円筒形のものであって、その外周面が入口筒4の外周面と面一である。その構成は、入口筒4の網材がそのまま下方に延出するものであってもよいし、入口筒4の網材とは別の部材(網材であっても、孔のない板材であってもよい)が接続されたものであってもよい。延出筒6の高さ(上下方向長さ)は、入口筒4の高さよりも僅かに高くなっている。
外筒5は、入口筒4及び延出筒6より一回り大きな円筒形で、その内周面が入口筒4及び延出筒6の外周面に摺接するものであって、上下方向に摺動自在となっており、外筒5の内周面と入口筒4及び延出筒6の外周面の間の摩擦抵抗力により、任意の上下位置で固定できる。また、外筒5の高さ(上下方向長さ)は、入口筒4の高さよりも僅かに高く、延出筒6の高さと略同じであり、さらに外筒5の側面部には孔がない。よって、図2(a)に示すように、外筒5を最も上側の位置(上端部が入口筒4のフランジ42に当接する位置)にすると、入口筒4の外周面が全て覆われ、網目41が全て塞がれた全閉状態となり、二次空気の取り込み量は0となる。一方、図2(b)に示すように、外筒5を最も下側の位置(延出筒6に重なる位置)にすると、入口筒4の外周面が全て露出し、網目41が全て開放された全開状態となり、二次空気の取り込み量は最大となる。そして、図1に示すように、外筒5を上下方向の中間位置にすると、入口筒4の外周面の、外筒5上端より上側部分のみが露出した状態となり、網目41が等間隔に形成されているから、網目41の露出面積は入口筒4の外周面の露出面積に比例し、すなわち二次空気の取り込み量は入口筒4の外周面の露出面積に比例した量となる。
As shown in FIG. 1, the granule introduction part 2 is connected to the lower part of the hopper 7 and includes a connecting pipe 3, an inlet cylinder 4, an outer cylinder 5, and an extending cylinder 6.
The connecting pipe 3 connects an inlet cylinder 4 and a conveying pipe 1 which will be described later. The connecting pipe 3 is a circular pipe having the same diameter as the conveying pipe 1 and has an upstream end facing upward and a downstream side. The downstream end is bent in the horizontal direction. At the upstream end of the connecting pipe 3, a funnel-shaped part 31 that spreads upward is formed, and the inner diameter area of the upper end of the funnel-shaped part 31 is 1 of the inner diameter area of the conveying pipe 1. .5 to 2.0 times.
The inlet cylinder 4 is made of a cylindrical mesh material, more specifically, a so-called punching metal in which through holes are formed at equal intervals over the circumferential direction and the height direction of a cylindrical metal plate, It is connected to the upstream side of the connecting pipe 3 via a funnel-shaped portion 31 (the lower end portion of the inlet tube 4 is welded and fixed to the upper end portion of the funnel-shaped portion 31), and the upper end portion of the funnel-shaped portion 31 Therefore, the outer diameter of the cross section is longer than that of the transport pipeline 1. The height (length in the vertical direction) of the inlet cylinder 4 is lower than the outer diameter of the inlet cylinder 4. Moreover, the mesh 41 (hole part) of the mesh material which comprises the inlet pipe | tube 4 is a thing smaller than the rice grain conveyed. Further, a flange 42 is formed at the upper end portion of the inlet cylinder 4, and the flange 71 of the hopper 7 is brought into contact with the flange 42 of the inlet cylinder 4 and screwed so that the hopper 7 is directly above the inlet cylinder 4. Connected. Secondary air is taken from the inlet cylinder 4 through the mesh 41. An extension cylinder 6 is provided below the inlet cylinder 4.
The extending tube 6 is a cylindrical member that extends further downward from the portion connected to the funnel-shaped portion 31 at the lower end of the inlet tube 4, and its outer peripheral surface is the outer periphery of the inlet tube 4. It is flush with the surface. The configuration may be such that the mesh material of the inlet cylinder 4 extends downward as it is, or a member different from the mesh material of the inlet cylinder 4 (even a mesh material is a plate material without holes. May be connected). The height (length in the vertical direction) of the extension tube 6 is slightly higher than the height of the inlet tube 4.
The outer cylinder 5 has a cylindrical shape that is slightly larger than the inlet cylinder 4 and the extension cylinder 6, and the inner peripheral surface thereof is in sliding contact with the outer peripheral surfaces of the inlet cylinder 4 and the extension cylinder 6, and slides in the vertical direction. It can be freely fixed at an arbitrary vertical position by the frictional resistance between the inner peripheral surface of the outer cylinder 5 and the outer peripheral surfaces of the inlet cylinder 4 and the extension cylinder 6. Further, the height (length in the vertical direction) of the outer cylinder 5 is slightly higher than the height of the inlet cylinder 4 and is substantially the same as the height of the extension cylinder 6, and there is a hole in the side surface of the outer cylinder 5. Absent. Therefore, as shown in FIG. 2A, when the outer cylinder 5 is set to the uppermost position (position where the upper end abuts against the flange 42 of the inlet cylinder 4), the entire outer peripheral surface of the inlet cylinder 4 is covered, and the mesh 41 is fully closed, and the amount of secondary air taken in becomes zero. On the other hand, as shown in FIG. 2 (b), when the outer cylinder 5 is at the lowest position (position overlapping the extension cylinder 6), the entire outer peripheral surface of the inlet cylinder 4 is exposed and all the mesh 41 is opened. The secondary air intake amount is maximized. Then, as shown in FIG. 1, when the outer cylinder 5 is set at an intermediate position in the vertical direction, only the upper part of the outer peripheral surface of the inlet cylinder 4 above the upper end of the outer cylinder 5 is exposed, and the mesh 41 is formed at equal intervals. Therefore, the exposed area of the mesh 41 is proportional to the exposed area of the outer peripheral surface of the inlet cylinder 4, that is, the amount of secondary air taken in is proportional to the exposed area of the outer peripheral surface of the inlet cylinder 4.

搬送管路1は、粒体導入部2の連結管3の水平に延びる下流側端部に接続された断面円形の配管であって、図3に示すように、下流側に向けて設置面近傍から屈曲して上方へ垂直に延び、さらに原料タンク15よりも高い位置で屈曲して水平に延びている。搬送管路1は鋼管からなるものであるが、垂直部分の一部が透明な樹脂製の管に置き換えられており、管内を目視可能な検視管11となっている。また、搬送管路1は、屈曲部分と直線部分とで別体の管材からなり、各管材及び検視管11の端部にフランジを設けてあって、各管材同士及び管材と検視管11との接合部は、フランジ同士をネジ止めすることで密閉性が確保されている。この搬送管路1の管内を、精米された米粒が空気流に乗せられて通過する。   The conveyance pipe line 1 is a pipe having a circular cross section connected to a downstream end part extending horizontally of the connecting pipe 3 of the granule introduction part 2, and as shown in FIG. 3, in the vicinity of the installation surface toward the downstream side. And bent vertically upward and further bent at a position higher than the raw material tank 15 and horizontally extended. Although the conveyance pipe line 1 is made of a steel pipe, a part of the vertical portion is replaced with a transparent resin pipe, and the inspection pipe 11 is formed so that the inside of the pipe can be visually observed. Moreover, the conveyance pipe line 1 consists of a separate pipe material in a bending part and a linear part, and has provided the flange in the edge part of each pipe material and the test tube 11, and each pipe material and pipe material and the test tube 11 are provided. The joint portion is secured by screwing the flanges together. The polished rice grains pass through the pipe of the conveying pipe 1 in an air flow.

空気分離減速システム12は、減速器121と、入口管122、出口管123及び支管124からなる。入口管122は、搬送管路1の水平に延びる下流側端部に接続されており、下流側に向けて水平に延び屈曲して下方斜め約45度の角度に向けて延びている。減速器121は、外管121aと内管121bからなる二重管構造のものであって、内管121bが入口管122の下流側端部に接続されており、外管121aがその周囲を密閉して覆っている。内管121bは網材からなり、網目は搬送される米粒よりも小さいものとなっている。出口管123は、減速器121の内管121bの下流側端部に接続されており、下流側に向けて下方斜め約45度の角度に向けて延び屈曲して下方へ垂直に延びている。支管124は、減速器121の外管121aの側面に接続されており、下流側に向けて下方斜め約45度の角度に向けて延び屈曲して下方へ垂直に延びている。この空気分離減速システム12は、支管124側から空気が吸引されるものであり、内管121bの網目を通して搬送管路1内の空気が吸引されるが、米粒は、網目を通れないので減速されつつ内管121bから出口管123へと向かう。   The air separation speed reduction system 12 includes a speed reducer 121, an inlet pipe 122, an outlet pipe 123, and a branch pipe 124. The inlet pipe 122 is connected to a horizontally extending downstream end portion of the conveyance pipe line 1, extends horizontally toward the downstream side, bends, and extends downward at an angle of about 45 degrees. The speed reducer 121 has a double tube structure including an outer tube 121a and an inner tube 121b. The inner tube 121b is connected to the downstream end of the inlet tube 122, and the outer tube 121a seals the periphery thereof. And covering. The inner tube 121b is made of a mesh material, and the mesh is smaller than the rice grain being conveyed. The outlet pipe 123 is connected to the downstream end portion of the inner pipe 121b of the speed reducer 121, extends toward the downstream at an angle of about 45 degrees obliquely, and bends and extends vertically downward. The branch pipe 124 is connected to the side surface of the outer pipe 121a of the speed reducer 121, extends toward the downstream side at an angle of about 45 degrees and bends and extends vertically downward. In this air separation speed reduction system 12, air is sucked from the side of the branch pipe 124, and air in the conveying pipe 1 is sucked through the mesh of the inner pipe 121b, but the rice grains are decelerated because they do not pass through the mesh. While going from the inner pipe 121b to the outlet pipe 123.

バグフィルタ13は、空気入口が支管124の下流側端部に接続されており、空気から米糠などのダスト(微粒子)を分離して下部のダストボックス131にため、ダストが除去された空気を空気出口から吸引装置14に吸引させるものである。ダストボックス131の下端部には開閉自在な蓋を設けてあり、稼働時には蓋が閉じられていてダストをため、停止時に適宜蓋を開いてダストを排出することができる。   The bag filter 13 has an air inlet connected to the downstream end of the branch pipe 124, and separates dust (fine particles) such as rice bran from the air into the lower dust box 131. To the suction device 14. A lid that can be freely opened and closed is provided at the lower end of the dust box 131. The lid is closed during operation, so that dust can be collected, and the dust can be discharged by opening the lid appropriately when stopped.

吸引装置14は、ブロワであって、吸引側が配管によりバグフィルタ13の空気出口に接続されており、排気側が大気解放されている。   The suction device 14 is a blower, the suction side is connected to the air outlet of the bag filter 13 by piping, and the exhaust side is open to the atmosphere.

ロータリバルブ17は、ケーシング内に放射状の回転羽根を設けたものであり、入口が空気分離減速システム12の出口管123の下流側端部に接続されている。回転羽根が、上流側と下流側の密閉性を保ちつつ回転して、米粒を定量ずつ出口へと繰り出すものである。そして、製品タンク18は、上部が円筒形であり、下部が漏斗状で下方に向けて窄まった形状であって、上部にロータリバルブ17の出口が接続されている。ロータリバルブ17から繰り出される米粒をためることができるものであり、下端部が開閉自在な構造となっていて、適宜ためた米粒を取り出すことができる。   The rotary valve 17 is provided with radial rotary blades in the casing, and the inlet is connected to the downstream end of the outlet pipe 123 of the air separation speed reduction system 12. The rotating blades rotate while maintaining the airtightness of the upstream side and the downstream side, and the rice grains are fed out to the outlet in a fixed amount. The product tank 18 has a cylindrical shape at the top, a funnel-like shape at the bottom and is narrowed downward, and the outlet of the rotary valve 17 is connected to the top. The rice grains fed out from the rotary valve 17 can be collected, and the lower end portion has a structure that can be freely opened and closed, so that the appropriate rice grains can be taken out.

次に、この空気吸引式搬送装置の動作について説明する。稼働時には、吸引装置14とともに、精米機16及びロータリバルブ17が駆動する。精米機16の駆動により、原料タンク15に貯留された玄米が順次精米されて、排出口161から排出される。排出された米粒は、ホッパ7を経由して、さらに粒体導入部2へと流入する(図1の黒矢印)。そして、吸引装置14の駆動により、バグフィルタ13及び空気分離減速システム12を介して、搬送管路1内の空気が下流側から吸引され、管内に上流側から下流側へと向かう空気流が形成される。米粒は、この空気流に乗って、搬送管路1内を上流側から下流側へと搬送される。この際、粒体導入部2の入口筒4から、搬送管路1内に二次空気が取り込まれ(図1の白矢印)、その取り込み量は、外筒5を上下に摺動させて入口筒4の外周面の露出面積を変化させることで調整できる。取り込まれた二次空気と米粒は均一に混ざり合って搬送管路1内を流れ(図1の白黒矢印)、さらに空気分離減速システム12へと流入する。空気分離減速システム12においては、減速器121の側面に接続された支管124により空気が吸引されるので、減速器121の下流側へ向かう空気流がなくなり、米粒が減速される。ここで、米粒と一緒に搬送された米糠などのダストは、減速器121の内管121bの網目を通り抜けて支管124へと吸引され、バグフィルタ13により捕集される。そして、減速された米粒は、空気分離減速システム12からロータリバルブ17へと流入し、回転羽根により定量ずつ繰り出されて製品タンク18に貯留される。   Next, the operation of this air suction type conveying apparatus will be described. During operation, the rice mill 16 and the rotary valve 17 are driven together with the suction device 14. By driving the rice mill 16, the brown rice stored in the raw material tank 15 is sequentially polished and discharged from the discharge port 161. The discharged rice grains further flow into the grain introduction part 2 via the hopper 7 (black arrow in FIG. 1). Then, by driving the suction device 14, the air in the conveyance pipeline 1 is sucked from the downstream side via the bag filter 13 and the air separation deceleration system 12, and an air flow from the upstream side to the downstream side is formed in the pipe. Is done. The rice grains are transported from the upstream side to the downstream side in the transport pipeline 1 on this air flow. At this time, secondary air is taken into the conveyance pipe line 1 from the inlet cylinder 4 of the granule introduction part 2 (white arrow in FIG. 1), and the intake amount is determined by sliding the outer cylinder 5 up and down. It can be adjusted by changing the exposed area of the outer peripheral surface of the tube 4. The taken-in secondary air and rice grains are uniformly mixed and flow through the transport pipe 1 (black and white arrow in FIG. 1), and further flow into the air separation deceleration system 12. In the air separation speed reduction system 12, air is sucked by the branch pipe 124 connected to the side surface of the speed reducer 121, so there is no air flow toward the downstream side of the speed reducer 121, and the rice grains are decelerated. Here, dust such as rice bran conveyed with the rice grains passes through the mesh of the inner pipe 121 b of the speed reducer 121 and is sucked into the branch pipe 124 and collected by the bag filter 13. Then, the slowed rice grains flow into the rotary valve 17 from the air separation speed reduction system 12, are fed out by a fixed amount by the rotary blades, and are stored in the product tank 18.

このように構成した本発明の空気吸引式搬送装置の第一実施形態によれば、精米機16の排出口161とホッパ7の間が異物混入防止のために密閉されており、ホッパ7の上流側からは十分な量の二次空気を取り込むことができないが、その代わりに、網材からなる入口筒4から二次空気を取り込むことが可能である。二次空気の量は、少なすぎると搬送管路1の途中で詰まりを生じるおそれがあり、多すぎると搬送終端部で米粒が十分に減速できずロータリバルブ17などに衝突して割れなどの被害が生じるおそれがあるため、米粒の供給量に応じて適宜調整する必要があるが、この第一実施形態では入口筒4の外周面に摺接する外筒5を摺動させて入口筒4の外周面の露出面積を変化させることで、二次空気の取り込み量を容易に調整可能である。この調整は、装置の稼働中に、搬送の状態を観察しながら行うこともできる。そして、入口筒4の網目41よりも大きな異物の混入は、確実に防ぐことができる。また、入口筒4が搬送管路1よりも大径で、断面の外周が長いので、同径の場合と比較して、入口筒4の表面積が同じ(=網目の総面積が同じ=二次空気の取り込み量が同じ)場合にその高さを低くできるので、結果として粒体導入部2全体を小型化できる。さらに、上から下へ通過する粒体に対して水平方向の全周から二次空気が取り込まれて均一に混ざり合うので、搬送効率が良い。また、入口筒4の下側に延出筒6を設けてあるので、この延出筒6部分に外筒5を摺動させることで、入口筒4の外周面の全体が露出し、二次空気の取り込み量を最大化できる。さらに、二次空気の取り込み箇所が搬送の入口部よりも下流側であると、搬送管路1内に先に米粒が流入し、重い米粒の層と軽い空気の層に分かれて均一に混ざり合わず搬送効率が低下してしまうが、この第一実施形態では粒体を導入するホッパ7と入口筒4が直結されているので、搬送の入口部から二次空気が供給され、米粒と空気が均一に混ざり合い搬送効率が良い。   According to the first embodiment of the air suction type conveying apparatus of the present invention configured as described above, the space between the discharge port 161 of the rice milling machine 16 and the hopper 7 is hermetically sealed to prevent foreign matter from entering, and the upstream of the hopper 7. A sufficient amount of secondary air cannot be taken in from the side, but instead, secondary air can be taken in from the inlet tube 4 made of a mesh material. If the amount of secondary air is too small, there is a risk of clogging in the middle of the conveyance pipeline 1, and if it is too large, the rice grains cannot sufficiently decelerate at the conveyance end and collide with the rotary valve 17 and cause damage such as cracks. However, in this first embodiment, the outer cylinder 5 slidably contacting the outer peripheral surface of the inlet cylinder 4 is slid and the outer periphery of the inlet cylinder 4 is adjusted. The amount of secondary air taken in can be easily adjusted by changing the exposed area of the surface. This adjustment can also be performed while observing the state of conveyance during operation of the apparatus. In addition, it is possible to reliably prevent foreign matters larger than the mesh 41 of the inlet cylinder 4 from being mixed. In addition, since the inlet cylinder 4 has a larger diameter than the conveying pipe 1 and the outer periphery of the cross section is longer, the surface area of the inlet cylinder 4 is the same (= the same total area of the mesh = secondary) as compared with the case of the same diameter When the air intake amount is the same), the height can be reduced, and as a result, the entire granule introduction unit 2 can be downsized. Furthermore, since the secondary air is taken in from the entire circumference in the horizontal direction to the particles passing from the top to the bottom and mixed uniformly, the conveyance efficiency is good. Further, since the extension cylinder 6 is provided below the inlet cylinder 4, the entire outer peripheral surface of the inlet cylinder 4 is exposed by sliding the outer cylinder 5 on the extension cylinder 6 portion, and the secondary cylinder Air intake can be maximized. Furthermore, if the secondary air intake location is downstream from the entrance of the conveyance, the rice grains first flow into the conveyance pipeline 1 and are divided into a heavy rice grain layer and a light air layer and mixed uniformly. However, in this first embodiment, since the hopper 7 for introducing the granule and the inlet cylinder 4 are directly connected, secondary air is supplied from the inlet of the conveyance, and the rice grains and the air are Uniform mixing and good transport efficiency.

次に、本発明の空気吸引式搬送装置の第二実施形態について、第一実施形態との相違点に絞って説明する。第二実施形態は、第一実施形態と比較して、粒体導入部2の外筒5の形状が異なっている。図4(a)に示すように、第二実施形態の外筒5は、第一実施形態のものと同径の筒状のものであって、上端の周方向の一部分がさらに上側へ延びていて、この部分が規制部51となっており、規制部51が存在しない部分が、上方に向けて開口する切欠部52となっている。規制部51は、凸形であって、周方向の複数箇所に設けてあり、それに伴い、切欠部52は、凹形であって、周方向の複数箇所に形成される。   Next, a second embodiment of the air suction type conveyance device of the present invention will be described focusing on differences from the first embodiment. 2nd embodiment differs in the shape of the outer cylinder 5 of the granule introduction part 2 compared with 1st embodiment. As shown in FIG. 4 (a), the outer cylinder 5 of the second embodiment is a cylinder having the same diameter as that of the first embodiment, and a part of the upper end in the circumferential direction further extends upward. Thus, this portion is the restricting portion 51, and the portion where the restricting portion 51 does not exist is a cutout portion 52 that opens upward. The restricting portion 51 has a convex shape and is provided at a plurality of locations in the circumferential direction, and accordingly, the cutout portion 52 has a concave shape and is formed at a plurality of locations in the circumferential direction.

この第二実施形態によれば、図4(a)に示すように、外筒5を最も上側の位置(規制部51の上端部が入口筒4のフランジ42に当接する位置で、規制部51によってこれより上側への移動が規制されている)にした場合でも、外筒5の上端5aが入口筒4の上端のフランジ42より下側となり、外筒5の上端5aと入口筒4の上端のフランジ42の間部分の切欠部52から入口筒4の外周面が露出し、当該部分の網目41が開放されるので、全閉状態とはならず、所定量の二次空気が取り込まれる。ホッパ7の上流側の密閉性が特に高い場合、入口筒4が全閉状態のまま装置を稼働させると、搬送管路1内の空気量が極端に不足して、搬送不能となり、吸引装置14を損傷するおそれもあるが、この第二実施形態では、入口筒4が全閉状態にならないので、それらを防ぐことができる。そしてその他の点においては、第一実施形態と同様の作用効果を奏する。   According to the second embodiment, as shown in FIG. 4A, the outer cylinder 5 is placed at the uppermost position (the position where the upper end of the restriction part 51 abuts against the flange 42 of the inlet cylinder 4). The upper end 5a of the outer cylinder 5 is located below the flange 42 at the upper end of the inlet cylinder 4, and the upper end 5a of the outer cylinder 5 and the upper end of the inlet cylinder 4 are restricted. Since the outer peripheral surface of the inlet cylinder 4 is exposed from the notch 52 between the flanges 42 and the mesh 41 of the part is opened, the secondary air is not fully closed but a predetermined amount of secondary air is taken in. When the upstream side of the hopper 7 has a particularly high sealing performance, if the apparatus is operated while the inlet cylinder 4 is fully closed, the amount of air in the transport pipe line 1 becomes extremely short and cannot be transported, and the suction device 14 However, in the second embodiment, the inlet tube 4 is not fully closed, and therefore can be prevented. And in other points, there exists an effect similar to 1st embodiment.

次に、本発明の空気吸引式搬送装置の第三実施形態について、第一実施形態との相違点に絞って説明する。第三実施形態は、第一実施形態と比較して、粒体導入部2の入口筒4に規制部43を設けた点が異なっている。図4(b)に示すように、第三実施形態の入口筒4は、第一実施形態のものと同じ大きさの網材からなる筒状のものであって、外周面の上端よりやや下側の位置に、外周側に向けて突出する規制部43を設けてある。規制部43は、略円柱形であって、周方向の1箇所に設けてある。   Next, a third embodiment of the air suction type conveyance device of the present invention will be described focusing on differences from the first embodiment. 3rd embodiment differs in the point which provided the control part 43 in the inlet cylinder 4 of the granule introduction part 2 compared with 1st embodiment. As shown in FIG. 4 (b), the inlet cylinder 4 of the third embodiment is a cylinder made of a net material having the same size as that of the first embodiment, and is slightly below the upper end of the outer peripheral surface. A restricting portion 43 that protrudes toward the outer peripheral side is provided at the side position. The restricting portion 43 has a substantially cylindrical shape and is provided at one place in the circumferential direction.

この第三実施形態によれば、図4(b)に示すように、外筒5の上端5aが規制部43に当接する位置が最も上側の位置(規制部43によってこれより上側への移動が規制されている)となり、この場合でも外筒5の上端5aが入口筒4の上端のフランジ42より下側となり、外筒5の上端5aと入口筒4の上端のフランジ42の間部分から入口筒4の外周面が露出し、当該部分の網目41が開放されるので、全閉状態とはならず、所定量の二次空気が取り込まれる。よって、この第三実施形態も、第二実施形態と同様の作用効果を奏する。   According to the third embodiment, as shown in FIG. 4B, the position at which the upper end 5a of the outer cylinder 5 abuts against the restricting portion 43 is the uppermost position (the restricting portion 43 moves upward from this position). Even in this case, the upper end 5a of the outer cylinder 5 is located below the flange 42 at the upper end of the inlet cylinder 4, and the inlet from the portion between the upper end 5a of the outer cylinder 5 and the flange 42 at the upper end of the inlet cylinder 4 is provided. Since the outer peripheral surface of the cylinder 4 is exposed and the mesh 41 of the portion is opened, the fully closed state is not achieved, and a predetermined amount of secondary air is taken in. Therefore, this third embodiment also has the same effects as the second embodiment.

なお、本発明の空気吸引式搬送装置において、二次空気の適切な取り込み量は、搬送物の種類、搬送工程(距離と高さ)及び搬送効率の条件に応じて、搬送管路の断面積を基準として、およその値が定まるものである。実験によれば、搬送物が米や麦などの穀粒である場合、搬送管路の断面積に対して、二次空気の取り込み面積(入口筒の網目部分の面積)は、最大で1.2倍までが理想的な調整範囲であり、これ以上取り込み面積を大きくすると、二次空気の取り込み量が過大となって、搬送終端部で搬送物を十分に減速できなくなってしまう。   In the air suction type conveying apparatus of the present invention, the appropriate amount of secondary air taken in depends on the type of conveyed item, conveying process (distance and height) and conveying efficiency. The approximate value is determined with reference to. According to the experiment, when the conveyed product is a grain such as rice or wheat, the area of secondary air intake (the area of the mesh portion of the inlet tube) is 1. The ideal adjustment range is up to twice, and if the intake area is made larger than this, the amount of secondary air taken in becomes excessive, and the conveyed product cannot be sufficiently decelerated at the conveyance end portion.

本発明は、上記の実施形態に限定されない。たとえば、各実施形態において、粒体導入部の連結管は、搬送管路と同径のものに限られず、搬送管路よりも内径面積が大きいものや小さいものであってもよい。そして、連結管と搬送管路の内径面積が異なる場合、両者は内径面積が漸減又は漸増する漏斗状の管により接続されることが望ましい。また、搬送管路、連結管、入口筒、外筒及び延出筒は、断面矩形など、断面円形以外の形状であってもよい。また、上下方向に摺動自在である外筒を入口筒及び延出筒に確実に固定するための固定部材を設けてもよい。固定部材の一例としては、いわゆるホースバンドのように、外筒を外周側から締め付けて固定するものが挙げられる。また、延出筒の下端部に、外周側に突出する突出部を設け、外筒を下向きに摺動させたときに外筒の下端部が突出部に当接するようにすることで、外筒が延出筒から脱落することを防ぐものであってもよい。この際、突出部は、延出筒の周方向の1箇所又は複数箇所に設けたものであってもよいし、周方向の全周にわたって設けた鍔状のものであってもよい。また、第二実施形態において、外筒に設ける規制部の形状はどのようなものであってもよく、周方向の少なくとも1箇所に設けてあればよい。さらに、第三実施形態において、入口筒に設ける規制部の形状はどのようなものであってもよく、周方向の複数箇所に設けたものでもよいし、周方向の全周にわたって設けた鍔状のものであってもよい。   The present invention is not limited to the above embodiment. For example, in each embodiment, the connecting pipe of the granule introduction part is not limited to the same diameter as the conveyance pipe line, and may have a larger or smaller inner diameter area than the conveyance pipe line. When the inner diameter areas of the connecting pipe and the conveying pipe line are different, it is desirable that both are connected by a funnel-shaped pipe whose inner diameter area gradually decreases or increases. Moreover, shapes other than circular cross-sections, such as a cross-sectional rectangle, may be sufficient as a conveyance pipe line, a connecting pipe, an entrance cylinder, an outer cylinder, and an extension cylinder. Moreover, you may provide the fixing member for fixing the outer cylinder which is slidable to an up-down direction to an entrance cylinder and an extension cylinder reliably. As an example of the fixing member, a member that fastens and fixes the outer cylinder from the outer peripheral side, such as a so-called hose band, can be mentioned. In addition, by providing a projecting portion that protrudes to the outer peripheral side at the lower end portion of the extended cylinder so that the lower end portion of the outer cylinder contacts the projecting portion when the outer cylinder is slid downward, the outer cylinder May be prevented from falling off the extension tube. In this case, the protruding portion may be provided at one or a plurality of locations in the circumferential direction of the extending cylinder, or may be a hook-like shape provided over the entire circumference in the circumferential direction. Moreover, in 2nd embodiment, what kind of shape of the control part provided in an outer cylinder may be sufficient, and it should just be provided in at least 1 place of the circumferential direction. Furthermore, in 3rd embodiment, what kind of shape of the control part provided in an inlet_tube | cylinder may be sufficient, the thing provided in the several places of the circumferential direction may be sufficient, and the bowl shape provided over the perimeter of the circumferential direction It may be.

1 搬送管路
2 粒体導入部
3 連結管
4 入口筒
5 外筒
6 延出筒
7 ホッパ
43 規制部
51 規制部

DESCRIPTION OF SYMBOLS 1 Conveyance pipe line 2 Granule introduction part 3 Connection pipe 4 Inlet cylinder 5 Outer cylinder 6 Extension cylinder 7 Hopper 43 Restriction part 51 Restriction part

Claims (5)

粒体が通過する搬送管路と、該搬送管路の上流側に接続する粒体導入部を備え、
該粒体導入部は、連結管と、入口筒と、外筒を備え、
前記連結管は、上流側端部が上方を向き、下流側端部が前記搬送管路に接続しており、
前記入口筒は、網材からなり前記連結管の上流側に接続しており、
前記外筒は、内周面が前記入口筒の外周面に摺接するものであって上下方向に摺動自在であることを特徴とする空気吸引式搬送装置。
A conveyance pipe line through which the granular material passes, and a granular material introduction section connected to the upstream side of the conveyance pipe line,
The granule introduction part includes a connecting tube, an inlet tube, and an outer tube,
The connecting pipe has an upstream end facing upward, and a downstream end connected to the transport pipeline,
The inlet cylinder is made of a mesh material and connected to the upstream side of the connecting pipe,
An air suction type conveying apparatus characterized in that the outer peripheral surface of the outer cylinder is in sliding contact with the outer peripheral surface of the inlet cylinder and is slidable in the vertical direction.
前記入口筒は、前記搬送管路より断面の外周が長いことを特徴とする請求項1記載の空気吸引式搬送装置。   The air suction type conveying apparatus according to claim 1, wherein the inlet cylinder has a longer outer periphery in cross section than the conveying pipe line. 前記入口筒の下側に延出筒を設けてあり、
該延出筒は、外周面が前記入口筒の外周面と面一であることを特徴とする請求項2記載の空気吸引式搬送装置。
An extending cylinder is provided below the inlet cylinder;
The air suction type transfer device according to claim 2, wherein the extended cylinder has an outer peripheral surface flush with an outer peripheral surface of the inlet cylinder.
前記入口筒又は前記外筒の何れか一方は、他方に当接して前記外筒の移動を規制する規制部を有しており、
該規制部は、前記外筒が、その上端が前記入口筒の上端より下側となる所定位置より上側へ移動することを規制するものであることを特徴とする請求項1、2又は3記載の空気吸引式搬送装置。
Either one of the inlet cylinder or the outer cylinder has a regulating portion that abuts the other and regulates the movement of the outer cylinder,
The said restriction | limiting part restrict | limits that the said outer cylinder moves to the upper side from the predetermined position in which the upper end is below the upper end of the said inlet cylinder, The said 1, 2 or 3 characterized by the above-mentioned. Air suction type transport device.
粒体を導入するホッパを備え、
該ホッパは、前記入口筒の直上に接続していることを特徴とする請求項1、2、3又は4記載の空気吸引式搬送装置。

Equipped with a hopper for introducing granules,
5. The air suction type conveying apparatus according to claim 1, wherein the hopper is connected immediately above the inlet cylinder.

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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000111445A (en) * 1998-10-05 2000-04-21 Mitsubishi Heavy Ind Ltd Particle-supplying device
JP2001261156A (en) * 2000-03-22 2001-09-26 Taiheiyo Cement Corp Ejector and particulate matter supply/transport device
JP2002265046A (en) * 2001-03-09 2002-09-18 Tsukasa Kogyo Kk Double structure hopper for pneumatic transportation of particulate
JP2017124887A (en) * 2016-01-12 2017-07-20 株式会社タイワ精機 Shutter apparatus for air suction type conveyance machine

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000111445A (en) * 1998-10-05 2000-04-21 Mitsubishi Heavy Ind Ltd Particle-supplying device
JP2001261156A (en) * 2000-03-22 2001-09-26 Taiheiyo Cement Corp Ejector and particulate matter supply/transport device
JP2002265046A (en) * 2001-03-09 2002-09-18 Tsukasa Kogyo Kk Double structure hopper for pneumatic transportation of particulate
JP2017124887A (en) * 2016-01-12 2017-07-20 株式会社タイワ精機 Shutter apparatus for air suction type conveyance machine

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