JP2024082084A - Air conveyance device for granule - Google Patents
Air conveyance device for granule Download PDFInfo
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- JP2024082084A JP2024082084A JP2022195800A JP2022195800A JP2024082084A JP 2024082084 A JP2024082084 A JP 2024082084A JP 2022195800 A JP2022195800 A JP 2022195800A JP 2022195800 A JP2022195800 A JP 2022195800A JP 2024082084 A JP2024082084 A JP 2024082084A
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- 239000008187 granular material Substances 0.000 title claims abstract description 97
- 238000003860 storage Methods 0.000 claims abstract description 40
- 238000000926 separation method Methods 0.000 claims abstract description 37
- 239000000843 powder Substances 0.000 claims description 130
- 239000012254 powdered material Substances 0.000 claims description 27
- 238000007599 discharging Methods 0.000 claims description 5
- 239000000428 dust Substances 0.000 description 13
- 238000011144 upstream manufacturing Methods 0.000 description 4
- 238000009434 installation Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 239000003570 air Substances 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 235000012041 food component Nutrition 0.000 description 1
- 239000005417 food ingredient Substances 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
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Abstract
Description
本発明は、エア搬送装置、特に粉粒体を投入、収容可能なホッパと、ホッパの下部に連設されてホッパ内の粉粒体を強制排出するロータリバルブと、粉粒体圧送用のエアを噴出可能なブロワと、ロータリバルブから排出された粉粒体にブロワからの噴出エアを合流させて出口管に向かわせる混相器とを備え、ブロワからの噴出エアを利用して出口管から、該出口管に連なる粉粒体搬送先まで粉粒体をエア搬送できるようにした粉粒体用エア搬送装置に関する。 The present invention relates to an air conveying device, in particular an air conveying device for powdered granular material, which comprises a hopper capable of feeding and storing powdered granular material, a rotary valve connected to the bottom of the hopper for forcibly discharging the powdered granular material from the hopper, a blower capable of ejecting air for pressurizing the powdered granular material, and a phase mixer that merges the air ejected from the blower with the powdered granular material discharged from the rotary valve and directs it toward an outlet pipe, and which uses the air ejected from the blower to air-transport the powdered granular material from the outlet pipe to a powdered granular material destination connected to the outlet pipe.
上記粉粒体用エア搬送装置は、例えば特許文献1に開示されるように従来公知であり、この公知のものでは、粉粒体を収納したフレキシブルコンテナバッグ等の袋を吊り上げてエア搬送装置のホッパ直上位置に置き、そこからホッパ内に粉粒体を直接落下、投入している。 The above-mentioned air conveying device for powder and granular material is known in the art, as disclosed in, for example, Patent Document 1. In this known device, a bag such as a flexible container bag containing powder and granular material is lifted and placed directly above the hopper of the air conveying device, and the powder and granular material is then dropped directly into the hopper.
特許文献1のエア搬送装置では、ホッパ内への粉粒体の投入形態が、上記したようにホッパ直上位置までフレキシブルコンテナバッグを吊るした状態で、同バッグからホッパ内に粉粒体を直接落下させるしかなく、投入形態が限られてしまう課題がある。 In the air conveying device of Patent Document 1, the only way to feed powder into the hopper is to hang a flexible container bag directly above the hopper as described above, and then drop the powder directly from the bag into the hopper, which limits the ways in which it can be fed.
本発明は、上記に鑑み提案されたもので、従来構造の課題を解決可能とした粉粒体用エア搬送装置を提供することを目的とする。 The present invention was proposed in light of the above, and aims to provide an air conveying device for powder and granular material that can solve the problems of conventional structures.
前記目的を達成するために、本発明は、粉粒体を投入、収容可能なホッパと、前記ホッパの下部に連設されて該ホッパ内の粉粒体を強制排出するロータリバルブと、粉粒体圧送用のエアを噴出可能なブロワと、前記ロータリバルブから排出された粉粒体に前記ブロワからの噴出エアを合流させて出口管に向かわせる混相器とを備え、前記噴出エアを利用して前記出口管から、該出口管に連なる粉粒体搬送先まで粉粒体をエア搬送できるようにした粉粒体用エア搬送装置において、前記ホッパ内に直接連通する分離室を内部に有する中空の分離機本体と、前記分離室又は前記ホッパ内に開口し且つ該ホッパ内に粉粒体を投入可能な投入口を一端に有して、前記分離機本体に設けられる投入管と、前記投入口から投入された粉粒体の流入を抑制可能として前記分離室に開口する排気口を有して、前記分離機本体に設けられる排気管と、前記投入管の他端に接続されて外部の粉粒体貯留部より粉粒体を該投入管に導入可能な導入管と、その導入管を通して前記外部の粉粒体貯留部より前記投入管側に粉粒体を流動させるエア流を発生可能なエア流発生装置とを備え、前記分離機本体は、前記ホッパの上端部に着脱可能に結合されることを第1の特徴とする。 In order to achieve the above object, the present invention provides an air conveying device for powder and granular material, which comprises a hopper capable of charging and storing powder and granular material, a rotary valve connected to the lower part of the hopper for forcibly discharging the powder and granular material in the hopper, a blower capable of ejecting air for compressing the powder and granular material, and a phase mixer for merging the air ejected from the blower with the powder and granular material discharged from the rotary valve and directing it toward an outlet pipe, and which is capable of air-transporting the powder and granular material from the outlet pipe to a powder and granular material conveying destination connected to the outlet pipe using the ejected air, the device comprising a hollow separator body having a separation chamber therein that is directly connected to the inside of the hopper, and a separator for separating the powder and granular material from the separation chamber or the hopper. The separator has a first feature that it is provided with an input pipe provided in the separator body and having an input port at one end that opens into the hopper and allows powder and granular material to be input into the hopper, an exhaust pipe provided in the separator body and having an exhaust port that opens into the separation chamber and can suppress the inflow of powder and granular material input from the input port, an introduction pipe connected to the other end of the input pipe and capable of introducing powder and granular material from an external powder and granular material storage section into the input pipe, and an air flow generator that can generate an air flow that causes powder and granular material to flow from the external powder and granular material storage section to the input pipe side through the introduction pipe. The separator body is detachably connected to the upper end of the hopper.
また本発明は、前記第1の特徴に加えて、前記投入口は、前記ホッパの開放上面に対向して下向きに配置され、また前記排気口は、前記投入口より上方に間隔をおいて配置されることを第2の特徴とする。 In addition to the first feature, the present invention has a second feature in that the inlet is disposed facing downward and opposite the open top surface of the hopper, and the exhaust port is disposed at a distance above the inlet.
また本発明は、第1又は第2の特徴に加えて、前記エア流発生装置は、前記排気管を通して前記分離室内のエアを吸引して外部に排出可能な吸引ブロワを含むことを第3の特徴とする。 In addition to the first or second feature, the present invention has a third feature in that the air flow generating device includes a suction blower that can suck air from within the separation chamber through the exhaust pipe and discharge it to the outside.
本発明及び本明細書において、「投入口から投入された粉粒体の流入を抑制可能」とは、投入口から投入された粉粒体の排気口への流入が確実に制限可能(即ち排気口への粉粒体の流入量がゼロ)である場合が含まれる事は元より、その流入が概ね制限可能(即ち上記流入量が僅少ないし少量)である場合も含まれる意味である。 In this invention and this specification, "capable of suppressing the inflow of powdered or granular material introduced from the inlet" not only includes cases where the inflow of powdered or granular material introduced from the inlet into the exhaust outlet can be reliably restricted (i.e., the amount of powdered or granular material introduced into the exhaust outlet is zero), but also includes cases where the inflow can be largely restricted (i.e., the amount of inflow is very small or a small amount).
本発明の第1の特徴によれば、分離機本体をホッパの上端部に結合した状態では、エア流発生装置が、導入管を通して外部の粉粒体貯留部より投入管側に粉粒体を流動させるエア流を発生させることで、粉粒体貯留部の粉粒体を、導入管及び投入管を経て分離室側にエア流と共に強制流動させ得るので、投入管の投入口よりホッパ内に投入可能となる。このとき、排気管の排気口は、投入口から投入された粉粒体の流入を抑制可能として分離室に開口していて、粉粒体の排気管側への混入が抑制されるため、投入口からホッパに効率よく粉粒体を投入可能となる。一方、分離機本体をホッパより取り外して、ホッパの上面を開放した状態では、粉粒体が収容されたフレキシブルコンテナバッグ等の袋又は容器を支持してホッパの直上に配置することで、そこからホッパ内に粉粒体を直接、落下投入することができる。 According to the first feature of the present invention, when the separator body is connected to the upper end of the hopper, the air flow generating device generates an air flow through the inlet pipe to move the powder from the external powder storage section to the input pipe, and the powder in the powder storage section can be forced to flow together with the air flow through the inlet pipe and the input pipe to the separation chamber, so that the powder can be input into the hopper from the input port of the input pipe. At this time, the exhaust port of the exhaust pipe opens into the separation chamber so as to suppress the inflow of the powder input from the input port, and the inflow of the powder into the exhaust pipe side is suppressed, so that the powder can be efficiently input into the hopper from the input port. On the other hand, when the separator body is removed from the hopper and the top surface of the hopper is opened, a bag or container such as a flexible container bag containing the powder can be supported and placed directly above the hopper, so that the powder can be directly dropped into the hopper from there.
このように分離機本体をホッパの上端部に装着するか取り外すかに応じて、ホッパ内への粉粒体の異なる2つの投入形態を容易に選択可能となるため、使い勝手が頗る良好となる。 In this way, two different feeding methods for powder and granular material into the hopper can be easily selected depending on whether the separator body is attached to or detached from the top end of the hopper, making it extremely easy to use.
また特に第2の特徴に加えて、投入口は、ホッパの開放上面に対向して下向きに配置され、また排気口は、投入口より上方に間隔をおいて配置されるので、排気口を下向きの投入口に対し単に上方に離して配置するだけの簡単な構造で、投入口から分離室に一緒に入った粉粒体及びエアを効率よく分離することができる。 In addition to the second feature, the inlet is positioned facing downwards, facing the open top surface of the hopper, and the exhaust port is positioned at a distance above the inlet, so that the powder and air that enter the separation chamber from the inlet can be efficiently separated with a simple structure that simply positions the exhaust port above and away from the downward-facing inlet.
また第3の特徴によれば、エア流発生装置は、排気管を通して分離室内のエアを吸引して外部に排出可能な吸引ブロワを含むので、分離機本体をホッパの上端部に結合した状態では、吸引ブロワが分離室内のエアを排気管を通して吸引して外部に排出することで、粉粒体貯留部の粉粒体を導入管を通して投入管側に吸引流動させるエア流を発生させることができ、その投入管の投入口よりホッパ内に投入可能となる。またそのエア流を発生させるブロワは排気管側に配置できて、導入管側には配備不要であるため、導入管の配管構成を単純化できて、導入管を用いた粉粒体の吸引作業性が高められる。 According to the third feature, the air flow generating device includes a suction blower that can suck air from within the separation chamber through the exhaust pipe and discharge it to the outside. When the separator body is connected to the upper end of the hopper, the suction blower sucks air from within the separation chamber through the exhaust pipe and discharges it to the outside, generating an air flow that sucks and flows the powder in the powder storage section through the introduction pipe toward the introduction pipe, and the powder can be fed into the hopper through the introduction port of the introduction pipe. In addition, since the blower that generates the air flow can be placed on the exhaust pipe side and does not need to be placed on the introduction pipe side, the piping configuration of the introduction pipe can be simplified, and the workability of sucking the powder using the introduction pipe is improved.
本発明の実施形態を、添付図面により以下に具体的に説明する。 Embodiments of the present invention are described in detail below with reference to the attached drawings.
先ず、図1~図6において、粉粒体搬送用のエア搬送装置Aは、粉粒体が集積、貯留される粉粒体貯留部C(例えば、図示例のようなコンテナ等の収容容器、フレキシブルコンテナバッグ等の袋)の粉粒体を粉粒体搬送先Z(例えばサイロ、貯留槽等の粉粒体収容設備)までエア搬送するために利用されるものであって、それは、設置面(例えば地面等)に定置、固定される中空且つ直方体状のハウジング1を主体とする。ハウジング1の少なくとも上壁1tは、他のハウジング要素(即ち四方の側壁1s)に対し従来周知の結合手段(図示せず)を以て着脱可能に結合される。 First, in Figures 1 to 6, the air conveying device A for conveying powder and granular material is used to air convey powder and granular material from a powder and granular material storage section C (for example, a storage vessel such as a container as shown in the illustrated example, or a bag such as a flexible container bag) where the powder and granular material is accumulated and stored, to a powder and granular material destination Z (for example, a powder and granular material storage facility such as a silo or a storage tank), and is mainly composed of a hollow rectangular parallelepiped housing 1 that is placed and fixed on an installation surface (for example, the ground, etc.). At least the top wall 1t of the housing 1 is detachably connected to other housing elements (i.e., the four side walls 1s) by conventionally known connecting means (not shown).
ハウジング1内には、図2で明らかなように、粉粒体を上方より投入、収容可能なホッパHと、ホッパHの下部に接続されてホッパH内の粉粒体を強制排出するロータリバルブRと、粉粒体圧送用のエアを噴出可能な搬送用ブロワ3と、ロータリバルブRから排出された粉粒体に搬送用ブロワ3からの噴出エアを合流させて出口管4に向かわせる混相器Mとが少なくとも収容、固定される。 As can be seen in FIG. 2, at least the following are housed and fixed within the housing 1: a hopper H that can be used to input and store powder from above; a rotary valve R that is connected to the bottom of the hopper H and forcibly discharges the powder from the hopper H; a conveying blower 3 that can eject air for compressing the powder; and a phase mixer M that merges the air ejected from the conveying blower 3 with the powder discharged from the rotary valve R and directs it toward the outlet pipe 4.
出口管4の出口(下流端)は、ハウジング1の一側壁1sに設けた側部開口1iに臨んでおり、この出口には、側部開口1iを通してハウジング1内に延びる接続管5の一端部(上流端)が、従来周知のジョイントJ1を介して着脱可能に接続、連通される。その接続管5の他端部(下流端)は、上記粉粒体搬送先Zに直接に、又は延長接続管5′を介して通じている。尚、側部開口1iは、ハウジング1の一側壁1sに開閉可能に設けた不図示の開閉蓋により、エア搬送装置Aの非使用時には塞がれる。 The outlet (downstream end) of the outlet pipe 4 faces a side opening 1i provided in one side wall 1s of the housing 1, and one end (upstream end) of a connecting pipe 5 extending into the housing 1 through the side opening 1i is detachably connected and communicated to this outlet via a joint J1 that is conventionally known. The other end (downstream end) of the connecting pipe 5 is connected directly to the powder/granular material transport destination Z or via an extension connecting pipe 5'. The side opening 1i is closed by an opening/closing lid (not shown) that is provided on one side wall 1s of the housing 1 so as to be able to be opened and closed when the air transport device A is not in use.
エア搬送装置Aは、搬送用ブロワ3からの噴出エアを利用して、出口管4や接続管5,5′内での粉粒体の排出流動を助勢し、粉粒体搬送先Zまで粉粒体をスムーズにエア搬送できるようにする。 The air conveying device A uses the air jetted from the conveying blower 3 to assist the discharge flow of the powder and granular material in the outlet pipe 4 and the connecting pipes 5, 5', allowing the powder and granular material to be smoothly conveyed by air to the powder and granular material destination Z.
而して、エア搬送の対象となる粉粒体としては、エア搬送が可能な程度に流動性がある無数の粒状体(例えば木質チップ、飼料等)又は粉状体(例えばセメント、粉状化学剤,粉状食材等)が含まれる。 The powders that can be transported by air include numerous granular materials (e.g., wood chips, feed, etc.) or powders (e.g., cement, powdered chemicals, powdered food ingredients, etc.) that are fluid enough to be transported by air.
ホッパHは、粉粒体を上方より投入可能な上向き且つ矩形状の入口Hiを上端に有したホッパ本体Hmを主要部としており、そのホッパ本体Hmは、下方が徐々に窄まる角筒状に形成され、これの開放下端が、後述するロータリバルブRの入口Riに従来周知のジョイントJ2を介して着脱可能に接続、連通される。またホッパHの開放下端には、粉粒体の通過は許容するが大きな異物の通過は阻止する網部材9が固定される。 The hopper H mainly consists of a hopper body Hm with an upward-facing rectangular inlet Hi at its upper end through which powder and granular material can be added from above. The hopper body Hm is formed in a rectangular tube shape that gradually narrows downward, and its open lower end is detachably connected and communicated with the inlet Ri of the rotary valve R (described below) via a joint J2 that is well known in the art. A mesh member 9 is fixed to the open lower end of the hopper H, which allows powder and granular material to pass through but prevents the passage of large foreign objects.
ハウジング1の上壁1tには、ホッパHの上端部が嵌合、支持される矩形状の上部開口1toが形成される。そして、この上部開口1toを縁取るように取り囲む平面視矩形状の取付板2が、これと上壁1tとの間にホッパHの上端部外周の外向きフランジHfを挟持した状態で、上壁1tの上面に重合、固定(例えば溶接、ボルト止め等)される。また取付板2及び上壁1tには、後述する複数の共締め用ボルトb1をそれぞれ貫通させる複数のボルト孔が、互いに周方向に間隔をおいて形成される。 A rectangular upper opening 1to is formed in the upper wall 1t of the housing 1, into which the upper end of the hopper H is fitted and supported. The mounting plate 2, which is rectangular in plan view and surrounds the upper opening 1to, is laminated and fixed (for example, by welding, bolting, etc.) to the upper surface of the upper wall 1t with the outward flange Hf of the outer periphery of the upper end of the hopper H sandwiched between the mounting plate 2 and the upper wall 1t. In addition, the mounting plate 2 and the upper wall 1t are formed with a number of bolt holes spaced apart from each other in the circumferential direction, through which a number of co-fastening bolts b1, described later, pass.
次にロータリバルブRの一例について具体的に説明すると、ロータリバルブRは、図2,図4で明らかなように、上端に入口Riを、また下端に出口Roをそれぞれ有するバルブハウジングHrと、そのバルブハウジングHr内に回転自在に収容、支持されるロータ10と、このロータ10を回転駆動するバルブモータ11とを備える。上記出口Roは、矩形状に形成されていて、後述する混相器Mの矩形状の入口Miに従来周知のジョイントJ3を介して着脱可能に接続、連通される。 Next, an example of a rotary valve R will be described in detail. As is clear from Figures 2 and 4, the rotary valve R comprises a valve housing Hr having an inlet Ri at the upper end and an outlet Ro at the lower end, a rotor 10 rotatably housed and supported within the valve housing Hr, and a valve motor 11 that drives the rotor 10 to rotate. The outlet Ro is formed in a rectangular shape, and is detachably connected and communicated with the rectangular inlet Mi of the phase mixer M described below via a joint J3 that is conventionally known.
尚、バルブハウジングHrは、ハウジング1の内壁に不図示の支持手段を介して固定、支持される。 The valve housing Hr is fixed and supported on the inner wall of the housing 1 via a support means (not shown).
上記ロータ10は、バルブハウジングHrに回転自在に支持されてその中心部に横切る回転軸部10aと、回転軸部10aの外周に放射状に突設された複数の羽根板部10bとを一体に有する。そして、このロータ10をバルブモータ11で回転駆動すれば、そのモータ回転速度に応じた排出流量で、ホッパH内へ投入された粉粒体を出口Ro側(従って混相器M内)に強制的に排出可能である。 The rotor 10 is integral with a rotating shaft 10a that is rotatably supported by the valve housing Hr and crosses its center, and a number of vane plate sections 10b that are radially protruded from the outer periphery of the rotating shaft 10a. When the rotor 10 is rotated by a valve motor 11, the powder and granular material put into the hopper H can be forcibly discharged to the outlet Ro side (and therefore into the phase mixer M) at a discharge flow rate that corresponds to the motor rotation speed.
混相器Mは、図2,図4で明らかなように、ロータリバルブRの出口Roに臨む入口Miを上端に有する角筒状の混相器本体21と、その混相器本体21の下部に中央部が一体的に結合(例えば溶接)されて略水平な円管部22とを備える。混相器本体21は、下方に向かうにつれて互いに接近するよう傾斜した前・後側壁211,212と、前・後側壁211,212の左右両側縁間を一体に接続する略鉛直の左・右側壁213,214とを主要部としていて、下窄まりで且つ上下端開放のボックス状に形成される。 2 and 4, the phase mixer M comprises a square cylindrical phase mixer body 21 having an inlet Mi at its upper end facing the outlet Ro of the rotary valve R, and a substantially horizontal circular tube section 22 whose central section is integrally joined (for example, welded) to the lower part of the phase mixer body 21. The phase mixer body 21 is mainly made up of front and rear side walls 211, 212 that are inclined so as to approach each other as they go downward, and substantially vertical left and right side walls 213, 214 that integrally connect the left and right side edges of the front and rear side walls 211, 212, and is formed in a box shape that tapers downward and is open at the top and bottom ends.
それら前後左右の側壁211~214の下端部は、円管部22の中央部周壁の上部を切欠くように形成した平面視矩形状の上向きの開口22oの開口縁部にそれぞれ気密に接続(例えば溶接)される。そして、上記開口22o直下の円管部22内が、ロータリバルブRから排出された粉粒体と、搬送用ブロア3から噴出して円管部22内を流れるエアとの合流部となる。尚、混相器本体21及び円管部22のうち少なくとも一方は、ハウジング1の内壁に不図示の支持手段を介して固定、支持される。 The lower ends of the front, rear, left and right side walls 211-214 are airtightly connected (for example, welded) to the opening edge of an upward opening 22o that is rectangular in plan view and formed by cutting out the upper part of the central peripheral wall of the circular pipe section 22. The inside of the circular pipe section 22 directly below the opening 22o forms a confluence area for the powder discharged from the rotary valve R and the air that is sprayed from the conveying blower 3 and flows inside the circular pipe section 22. At least one of the phase mixer main body 21 and the circular pipe section 22 is fixed and supported by the inner wall of the housing 1 via a support means (not shown).
円管部22の一端(上流端)には、ハウジング1の内壁適所に固定した搬送用ブロワ3から延出するエア導入管23の下流端が従来周知のジョイントJ4を介して接続、連通される。一方、円管部22の他端(下流端)には、前述の出口管4の入口端が従来周知のジョイントJ5を介して着脱可能に接続、連通される。 One end (upstream end) of the circular pipe section 22 is connected and communicated with the downstream end of the air introduction pipe 23 extending from the conveying blower 3 fixed at an appropriate position on the inner wall of the housing 1 via a conventionally known joint J4. On the other hand, the other end (downstream end) of the circular pipe section 22 is detachably connected and communicated with the inlet end of the aforementioned outlet pipe 4 via a conventionally known joint J5.
エア搬送装置Aのハウジング1には、図示はしないが、搬送用ブロワ3及びロータリバルブR(具体的にはブロワモータ31及びバルブモータ11)、並びに後述する集塵機S(具体的には吸引ブロワ36のモータ36a)を作動させるための電源装置及び制御装置が収納される。尚、それらモータ31,11,36aを油圧作動式のモータでそれぞれ構成してもよい。 The housing 1 of the air conveying device A contains a power supply and a control device for operating the conveying blower 3 and the rotary valve R (specifically, the blower motor 31 and the valve motor 11), as well as the dust collector S (specifically, the motor 36a of the suction blower 36), which will be described later, although these are not shown. Note that the motors 31, 11, and 36a may each be configured as hydraulically operated motors.
以上説明したエア搬送装置Aの構成は、粉粒体用エア搬送装置として従来周知であって、例えば前記特許文献1にも開示されているが、本発明は、このようなエア搬送装置Aに、次に説明する吸引投入装置KTを着脱可能に付設した点を技術的特徴としている。この吸引投入装置KTは、これをエア搬送装置Aにセットした状態では、粉粒体貯留部Cがエア搬送装置AのホッパHから離れていても、そこから粉粒体を吸引してホッパH内に難なく投入可能とするための装置である。次に、図1~図3,図5及び図6を主として参照して、吸引投入装置KTの一例を説明する。 The configuration of the air conveying device A described above is conventionally known as an air conveying device for powdered or granular material, and is disclosed, for example, in the aforementioned Patent Document 1. However, the technical feature of the present invention is that a suction feed device KT, which will be described next, is detachably attached to such an air conveying device A. When this suction feed device KT is set on the air conveying device A, even if the powdered or granular material storage section C is separated from the hopper H of the air conveying device A, it is possible to suck up the powdered or granular material from there and easily feed it into the hopper H. Next, an example of the suction feed device KT will be described mainly with reference to Figures 1 to 3, 5, and 6.
吸引投入装置KTは、粉粒体貯留部Cよりエアと共に吸引される粉粒体からエアを分離してホッパH内に投入するための分離機30と、その分離機30で粉粒体より分離したエアを吸引して外部に排出可能な吸引排気装置ADとを備える。而して、吸引排気装置ADは、導入管Iを通して外部の粉粒体貯留部Cより投入管T側に粉粒体を流動させるエア流を発生可能な本発明のエア流発生装置の一例である。 The suction feed device KT is equipped with a separator 30 for separating the air from the powder and granular material sucked together with the air from the powder and granular material storage section C and feeding the air into the hopper H, and a suction and exhaust device AD that can suck the air separated from the powder and granular material by the separator 30 and discharge it to the outside. The suction and exhaust device AD is an example of an air flow generating device of the present invention that can generate an air flow that moves the powder and granular material from the external powder and granular material storage section C to the feed tube T through the introduction tube I.
分離機30は、ホッパH内に連通する分離室33を内部に有してホッパHの上端部に着脱可能に結合される中空のボックス状(実施形態は直方体状)の分離機本体31と、分離室33に開口し且つホッパHに粉粒体を投入可能な投入口Toを一端に有して、分離機本体31に設けられる投入管Tと、投入口Toから投入された粉粒体の吸引を抑制可能として分離室33に開口する排気口Doを有して分離機本体31に設けられる排気管Dとを備える。 The separator 30 is equipped with a hollow box-shaped (rectangular in the embodiment) separator body 31 that has a separation chamber 33 inside that communicates with the inside of the hopper H and is detachably connected to the upper end of the hopper H, an input pipe T provided in the separator body 31 that has an input port To at one end that opens into the separation chamber 33 and allows powdered material to be input into the hopper H, and an exhaust pipe D provided in the separator body 31 that has an exhaust port Do that opens into the separation chamber 33 and can suppress the suction of the powdered material input from the input port To.
分離機本体31は、これの開放下端が矩形状に形成されていて、ホッパH上端の入口Hi(従ってハウジング1の上壁1tの上部開口1to)と略同一形状に形成される。分離機本体31の下端部外周には外向きフランジ31fが連設されており、これら外向きフランジ31fは、上壁1t及びこれに固定の前記取付板2に複数のボルトb1を介して着脱可能に結合される。この場合、上壁1tの下面には、ボルトb1を螺合させるナットn1が固定(例えば溶接)されている。 The separator body 31 has an open lower end formed in a rectangular shape, and is formed in approximately the same shape as the inlet Hi at the upper end of the hopper H (and therefore the upper opening 1to of the upper wall 1t of the housing 1). Outward flanges 31f are connected to the outer periphery of the lower end of the separator body 31, and these outward flanges 31f are detachably connected to the upper wall 1t and the mounting plate 2 fixed thereto via multiple bolts b1. In this case, nuts n1 that screw onto the bolts b1 are fixed (for example, welded) to the underside of the upper wall 1t.
投入管Tの一端に開口する投入口Toは、ホッパHの開放上面(即ち入口Hi)に対向して下向きに配置される。その下向き配置のために投入管Tの、分離室33を横切る中間部は、下側に滑らかに彎曲した円弧状に折り曲げ形成される。 The feed inlet To, which opens at one end of the feed tube T, is arranged facing downward and opposite the open top surface (i.e., the inlet Hi) of the hopper H. To face downward, the middle part of the feed tube T that crosses the separation chamber 33 is bent downward into a smoothly curved arc shape.
また投入管Tの他端部は、分離機本体31の一側壁31sを貫通して外方に延出し且つその一側壁31sに固定(例えば溶接、ねじ止め等)される。そして、その一側壁1sの外方に張出す投入管Tの開口端には、外部の粉粒体貯留部Cより粉粒体を投入管Tに吸引導入可能な導入管Iの下流端が、従来周知のジョイントJ6を介して着脱可能に接続、連通される。 The other end of the input pipe T extends outward through one side wall 31s of the separator body 31 and is fixed (for example, welded, screwed, etc.) to that side wall 31s. The downstream end of the input pipe I, which can suck and introduce powder from an external powder/granular material storage section C into the input pipe T, is detachably connected and communicated with the open end of the input pipe T extending outward from the one side wall 1s via a conventionally known joint J6.
導入管Iの上流端は、これを粉粒体貯留部Cの粉粒体群に近接、対向させることで粉粒体を吸込み可能な吸込口として機能する。また導入管Iには、吸込み作業を無理なく行い得るように適度な可撓性が付与されることが望ましい。 The upstream end of the inlet pipe I functions as a suction port capable of sucking in the powder by being placed close to and facing the powder in the powder storage section C. It is also desirable that the inlet pipe I be given a suitable degree of flexibility so that the suction operation can be performed without difficulty.
また前記した排気口Doは、分離機本体31において、投入口Toから投入された粉粒体の排気口Doへの吸引・混入を抑制し得るよう投入口Toから上方に十分離れた位置に配置される。その排気口Doは、例えば分離機本体31の他側壁31s′に固定されてその内外を貫通する排気筒34により形成される。この排気筒34の外端部には、可撓性を有した排気チューブ35の上流端が従来周知のジョイントJ7を介して接続、連通される。そして、排気チューブ35の下流側に連なる集塵機Sが、ハウジング1周辺の設置面(例えば地面等)に設置、固定される。 The exhaust port Do is located in the separator body 31 at a position sufficiently above the inlet To to prevent the powder fed from the inlet To from being sucked into or mixed in with the exhaust port Do. The exhaust port Do is formed by, for example, an exhaust tube 34 fixed to the other side wall 31s' of the separator body 31 and penetrating the inside and outside of the wall. The upstream end of a flexible exhaust tube 35 is connected and communicated with the outer end of the exhaust tube 34 via a joint J7 that is well known in the art. The dust collector S connected to the downstream side of the exhaust tube 35 is installed and fixed to the installation surface (e.g., the ground) around the housing 1.
集塵機Sは、排気チューブ35の下流端に従来周知のジョイントJ8を介して着脱可能に接続、連通される吸込口36iを有して分離室33内のエアを吸引可能な吸引ブロワ36と、この吸引ブロワ36の吐出口36oに従来周知のジョイントJ9を介して着脱可能に接続、連通される袋状の集塵フィルタ37とを備える。そして、吸引ブロワ36が分離室33より吸引したエアは、集塵フィルタ37で濾過・清浄化された上で大気に排出される。尚、使用に伴い集塵フィルタ37内に集められた粉塵等は、随時の清掃作業で除かれる。 The dust collector S is equipped with a suction blower 36 having an inlet 36i that is detachably connected and communicated with the downstream end of the exhaust tube 35 via a conventionally known joint J8 and capable of sucking in air from the separation chamber 33, and a bag-shaped dust collection filter 37 that is detachably connected and communicated with the outlet 36o of the suction blower 36 via a conventionally known joint J9. The air sucked in from the separation chamber 33 by the suction blower 36 is filtered and purified by the dust collection filter 37 before being discharged into the atmosphere. Dust and other particles that collect in the dust collection filter 37 during use are removed by cleaning as needed.
而して、吸引ブロワ36を含む集塵機Sと、排気チューブ35とは互いに協働して前記吸引排気装置ADを構成する。この場合、吸引排気装置ADは、後述するように吸引ブロワ36で分離室33内のエアを吸引することで、エア搬送装置Aから離れた粉粒体貯留部Cの粉粒体を導入管Iを経て投入管Tに吸引して投入口ToよりホッパHに投入可能とするためのものである。この吸引排気装置ADの機能用途を踏まえ、吸引ブロワ36は、粉粒体貯留部Cから導入管Iを経て投入管Tに粉粒体を吸引し得るに足る十分大きい容量(換言すれば吸引力)のブロワが使用される。 The dust collector S including the suction blower 36 and the exhaust tube 35 cooperate to form the suction exhaust device AD. In this case, the suction exhaust device AD is designed to suck air from the separation chamber 33 with the suction blower 36 as described below, so that the powder in the powder storage section C away from the air conveying device A can be sucked into the input tube T via the introduction tube I and input into the hopper H from the input port To. In consideration of the functional use of the suction exhaust device AD, the suction blower 36 is a blower with a capacity (in other words, suction power) large enough to suck the powder from the powder storage section C through the introduction tube I into the input tube T.
尚、吸引ブロワ36の吸込口36iを排気筒34に直接(即ち排気チューブ35を介さずに)接続することで、排気筒34に集塵機Sを直結するようにしてもよい。 The suction port 36i of the suction blower 36 may be connected directly to the exhaust pipe 34 (i.e., without passing through the exhaust tube 35), thereby connecting the dust collector S directly to the exhaust pipe 34.
次に前記実施形態の作用について説明する。 Next, the operation of the above embodiment will be described.
エア搬送装置Aは、これに吸引投入装置KTを取付けて使用する場合(図1~図3を参照)と、吸引投入装置KTを取り外して使用する場合(図7,図8を参照)の2通りの使用態様を有する。 The air transport device A can be used in two ways: with the suction feed device KT attached (see Figures 1 to 3), or with the suction feed device KT removed (see Figures 7 and 8).
そこで先ず、前者の場合の使用態様について図1~図3を参照して説明する。この場合は、エア搬送装置Aの使用に際して、ハウジング1内の前記制御装置の操作部を操作して搬送用ブロワ3、ロータリバルブR及び集塵機Sをそれぞれ起動させる。 First, the former use will be described with reference to Figures 1 to 3. In this case, when using the air conveying device A, the operation unit of the control device in the housing 1 is operated to start the conveying blower 3, the rotary valve R, and the dust collector S.
特に集塵機S(具体的には吸引ブロワ36)の起動によれば、分離機本体31内の分離室33(延いては投入管T及び導入管I)内のエアが排気筒34及び排気チューブ35を経て吸引ブロワ36により吸引される。従って、導入管Iの外端開口を粉粒体貯留部Cの粉粒体群に近づけることで、吸引粉粒体貯留部Cの粉粒体を導入管Iを経て投入管Tに吸引できるため、その吸引された粉粒体が投入管Tの投入口ToよりホッパHに連続的に投入される。 In particular, when the dust collector S (specifically the suction blower 36) is started, the air in the separation chamber 33 (and thus the input pipe T and the introduction pipe I) in the separator body 31 is sucked in by the suction blower 36 through the exhaust pipe 34 and the exhaust tube 35. Therefore, by bringing the outer end opening of the introduction pipe I close to the powder mass in the powder storage section C, the powder in the suction powder storage section C can be sucked into the input pipe T through the introduction pipe I, and the sucked powder is continuously fed into the hopper H from the input port To of the input pipe T.
そして、ホッパH内に投入、収容された粉粒体は、ロータリバルブRにより混相器Mの入口Miまで強制排出され、混相器本体21内を流下する。 The powder and granular material that is placed in the hopper H is then forcibly discharged by the rotary valve R to the inlet Mi of the phase mixer M, and flows down through the phase mixer main body 21.
一方、搬送用ブロワ3の起動に伴い、同ブロワ3から噴出するエアがエア導入管23を通して混相器Mの円管部22の一端に勢いよく流入し、このエアは、円管部22内を通過して出口管4に向かう。 Meanwhile, when the conveying blower 3 is started, the air that is ejected from the blower 3 flows vigorously through the air inlet pipe 23 into one end of the circular pipe section 22 of the mixer M, and this air passes through the circular pipe section 22 toward the outlet pipe 4.
従って、ロータリバルブRから混相器本体21内に排出された粉粒体は、円管部22内で搬送用ブロワ3からのエアと合流して出口管4内に向かって流れ、このとき粉粒体がエアで助勢されて出口管4や接続管5,5′の内部をスムーズに流動するため、粉粒体供給先Zまでスムーズに供給される。 The powder discharged from the rotary valve R into the mixer body 21 merges with the air from the conveying blower 3 inside the circular pipe section 22 and flows toward the outlet pipe 4. At this time, the powder flows smoothly inside the outlet pipe 4 and the connecting pipes 5, 5' with the help of the air, so that it is supplied smoothly to the powder supply destination Z.
次に、エア搬送装置Aより吸引投入装置KTを取り外した状態での使用態様を図7,図8を参照して説明する。 Next, the usage mode when the suction feed device KT is removed from the air transport device A will be explained with reference to Figures 7 and 8.
この場合は、吸引投入装置KTの分離機本体31をエア搬送装置Aのハウジング1より取外し、これにより、ホッパHの入口Hiが図7で明らかなように、開放状態となる。この状態より、図8に例示したように、粉粒体を収容した袋B(例えばフレキシブルコンテナバッグ等)下部の排出筒部Baを、上方よりホッパH内に差し入れる。その袋Bは、例えば運搬車両等でエア搬送装置Aの近くまで輸送し、支持手段CL(例えばクレーン等の吊り上げ装置)で吊り上げて、ホッパHの真上に移動させる。次いで、それまで閉じ紐等の閉塞具(図示せず)で縛って閉じていた排出筒部Baを開くと、袋B内の粉粒体を自重でホッパH内に落下投入することができる。 In this case, the separator body 31 of the suction feed device KT is removed from the housing 1 of the air conveying device A, and the inlet Hi of the hopper H is opened as shown in FIG. 7. From this state, the discharge tube portion Ba at the bottom of the bag B (e.g., a flexible container bag, etc.) containing the powder or granular material is inserted from above into the hopper H, as shown in FIG. 8. The bag B is transported, for example, by a transport vehicle, close to the air conveying device A, and lifted by a support means CL (e.g., a lifting device such as a crane) and moved directly above the hopper H. Next, the discharge tube portion Ba, which had been tied and closed with a closing device such as a string (not shown), is opened, and the powder or granular material in the bag B can fall into the hopper H under its own weight.
それと並行して、エア搬送装置Aの搬送用ブロワ3やロータリバルブRを作動させておけば、ホッパH内に投入された粉粒体が、エア搬送装置Aによって前述と同様のエア助勢作用で出口管4及び接続管5,5′を経て粉粒体供給先Zまでスムーズに流動、供給される。 At the same time, if the conveying blower 3 and rotary valve R of the air conveying device A are operated, the powder and granular material fed into the hopper H will flow smoothly and be supplied to the powder and granular material supply destination Z through the outlet pipe 4 and connecting pipes 5, 5' by the air conveying device A with the same air assist action as described above.
以上説明した実施形態において、エア搬送装置Aに付設される吸引投入装置KTは、分離室33を内部に有してホッパHの上端部に着脱可能に結合される分離機本体31と、分離室33に開口し且つホッパH内に粉粒体を投入可能な投入口Toを一端に有して分離機本体31に設けられる投入管Tと、投入口Toから投入された粉粒体の排気口Doへの吸引を抑制可能として分離室33に開口する排気口Doを有して分離機本体31に設けられる排気管Dと、排気管Dを通して分離室33内のエアを吸引して外部に排出可能な吸引排気装置ADとを備え、投入管Tの他端には、外部の粉粒体貯留部Cより粉粒体を投入管Tに吸引導入可能な導入管Iが接続される。 In the embodiment described above, the suction feed device KT attached to the air conveying device A includes a separator body 31 having a separation chamber 33 therein and detachably connected to the upper end of the hopper H, a feed tube T provided on the separator body 31 and having an inlet To at one end that opens into the separation chamber 33 and allows powdered material to be fed into the hopper H, an exhaust pipe D provided on the separator body 31 and having an exhaust port Do that opens into the separation chamber 33 and prevents the powdered material fed from the inlet To from being sucked into the exhaust port Do, and a suction exhaust device AD that can suck air from the separation chamber 33 through the exhaust pipe D and discharge it to the outside. An introduction pipe I that can suck and introduce powdered material from an external powdered material storage section C into the feed tube T is connected to the other end of the feed tube T.
これにより、分離機本体31を図1~図3に例示したようハウジング1の上壁1t(従ってホッパHの上端部)に結合した状態では、吸引排気装置AD(吸気ブロワ36)が分離機本体31内の分離室33のエアを排気管Dから吸引して外部に排出することで、粉粒体貯留部Cの粉粒体を導入管Iを通して投入管T側に強制流動させるエア流が発生する。そして、このエア流によって、粉粒体貯留部Cの粉粒体を導入管I及び投入管Tを経て分離室33に吸引できるから、その吸引した粉粒体を投入管Tの投入口ToよりホッパH内に強制的に投入可能となる。 As a result, when the separator body 31 is connected to the upper wall 1t of the housing 1 (and therefore the upper end of the hopper H) as shown in Figures 1 to 3, the suction and exhaust device AD (suction blower 36) sucks air from the separation chamber 33 inside the separator body 31 through the exhaust pipe D and discharges it to the outside, generating an air flow that forces the powder and granular material in the powder and granular material storage section C to flow through the introduction pipe I and the introduction pipe T. This air flow then sucks the powder and granular material in the powder and granular material storage section C into the separation chamber 33 through the introduction pipe I and the introduction pipe T, so that the sucked powder and granular material can be forcibly introduced into the hopper H through the introduction port To of the introduction pipe T.
このとき、排気管Dの排気口Doは、投入口ToからホッパH側へ投入された粉粒体の排気口Doへの吸引を抑制可能な、投入口Toから離れた位置に配置されていて、その粉粒体の排気管D側への吸引が抑制される。そのため、投入口Toから分離室33に入った粉粒体及びエアのうち、殆どエアのみを吸引排気装置ADで外部に吸引排出できるから、ホッパH内に粉粒体を効率よく投入可能となる。 At this time, the exhaust port Do of the exhaust pipe D is located at a position away from the inlet To, which can prevent the powdered material fed from the inlet To into the hopper H from being sucked into the exhaust port Do, and the powdered material is prevented from being sucked into the exhaust pipe D. Therefore, of the powdered material and air that enter the separation chamber 33 from the inlet To, almost only the air can be sucked and discharged to the outside by the suction and exhaust device AD, so that the powdered material can be efficiently fed into the hopper H.
一方、図7,図8に例示したように、分離機本体31をハウジング1の上壁1t(従ってホッパHの上端部)より取外してホッパHの上面を開放した状態では、フレキシブルコンテナバッグ等の袋Bを吊るしてホッパHの直上に配置することで、そこからホッパH内に粉粒体を直接、落下投入することができる。 On the other hand, as shown in Figures 7 and 8, when the separator body 31 is removed from the upper wall 1t of the housing 1 (and therefore the upper end of the hopper H) and the top surface of the hopper H is opened, a bag B such as a flexible container bag can be hung and placed directly above the hopper H, and the powdered material can be dropped directly into the hopper H.
このように分離機本体31をハウジング1(従ってホッパH)の上端部に取付けるか取外すかに応じて、ホッパH内への粉粒体の異なる2つの投入形態を容易に選択可能となるため、使い勝手が頗る良好となる。 In this way, depending on whether the separator body 31 is attached to or detached from the upper end of the housing 1 (and therefore the hopper H), two different feeding methods for powder and granular material into the hopper H can be easily selected, making the device extremely easy to use.
また実施形態の分離機本体31は、中空の直方体状に形成され、投入口Toは、ホッパHの開放上面に対向して下向きに配置され、また排気管Dの排気口Doは、投入口Toより上方に間隔をおいて配置される。これにより、分離機本体31が単純構造のボックス状に形成されても、排気口Doを下向きの投入口Toに対し単に上方に離して配置するだけの簡単な構造で、投入口Toから分離室33に一緒に入った粉粒体及びエアを効率よく分離することができる。 The separator body 31 of the embodiment is formed in a hollow rectangular parallelepiped shape, the inlet To is arranged facing downwards facing the open top surface of the hopper H, and the exhaust outlet Do of the exhaust pipe D is arranged at a distance above the inlet To. As a result, even if the separator body 31 is formed in a simple box shape, the powder and granular material and air that enter the separation chamber 33 from the inlet To can be efficiently separated with a simple structure in which the exhaust outlet Do is simply arranged above and away from the downward-facing inlet To.
また実施形態では、導入管Iを通して外部の粉粒体貯留部Cより投入管T側に粉粒体を流動させるエア流を発生可能なエア流発生装置として、特に排気管Dを通して分離室33内のエアを吸引して外部に排出可能な吸引ブロワ36を主要部とするエア吸引排気装置ADが用いられる。これにより、上記エア流を発生させるブロワ(即ち吸引ブロワ36)は、排気管D側に配置できて、導入管I側には配備不要であるため、導入管Iの配管構成を頗る単純化できて、導入管Iを用いた粉粒体の吸引作業性が高められる。 In the embodiment, an air suction and exhaust device AD is used as an air flow generating device capable of generating an air flow that causes the powder to flow from the external powder storage section C to the input tube T through the introduction tube I. The air suction and exhaust device AD mainly comprises a suction blower 36 that can suck air from the separation chamber 33 through the exhaust tube D and exhaust it to the outside. As a result, the blower that generates the air flow (i.e., the suction blower 36) can be placed on the exhaust tube D side and does not need to be placed on the introduction tube I side, which greatly simplifies the piping configuration of the introduction tube I and improves the efficiency of the powder suction operation using the introduction tube I.
以上、本発明の実施形態について説明したが、本発明はその実施形態に限定されることなく、本発明の範囲内で種々の実施形態を実施可能である。 Although an embodiment of the present invention has been described above, the present invention is not limited to this embodiment, and various embodiments can be implemented within the scope of the present invention.
例えば、前記実施形態では、エア搬送装置Aが地面又は固定物(例えば建物等)の所定位置に固定的に設置される定置式のエア搬送装置Aであるものを例示したが、本発明のエア搬送装置は、定置式に限定されず、移動体(例えば車両)上に設置されて移動体と共に移動可能なものであってもよい。 For example, in the above embodiment, the air conveying device A is a stationary air conveying device A that is fixedly installed at a predetermined position on the ground or a fixed object (e.g., a building, etc.), but the air conveying device of the present invention is not limited to being a stationary device, and may be installed on a moving object (e.g., a vehicle) and movable together with the moving object.
また前記実施形態では、吸引投入装置KTの吸引対象となる粉粒体が収容された粉粒体貯留部Cとしてコンテナを例示したが、粉粒体貯留部Cは、実施形態に限定されない。例えば、コンテナ以外の粉粒体貯留容器や、フレキシブルコンテナバッグ等の袋が粉粒体貯留部であってもよく、或いは、地面等に山積みされた粉粒体貯留場所が粉粒体貯留部であってもよい。 In the above embodiment, a container is used as an example of the powder storage section C that contains the powder to be sucked by the suction feed device KT, but the powder storage section C is not limited to the embodiment. For example, a powder storage container other than a container, or a bag such as a flexible container bag, may be the powder storage section, or a powder storage location piled up on the ground, etc. may be the powder storage section.
また前記実施形態では、エア搬送装置Aから出口管4や接続管5を経て搬出される粉粒体搬送先Zとしてサイロ、貯留槽等の粉粒体収容設備を例示したが、粉粒体収容設備は、少なくとも粉粒体を一時的に収容して外部に取出し可能な設備であればよく、実施形態に限定されない。またこのような粉粒体収容設備を用いずに地面に野積み状態で粉粒体を仮置きしてもよく、この場合は、当該地面が粉粒体搬送先Zとなる。 In the above embodiment, a powder storage facility such as a silo or storage tank is exemplified as the powder destination Z for the powder transported from the air transport device A through the outlet pipe 4 and the connecting pipe 5, but the powder storage facility is not limited to the embodiment as long as it is at least a facility that can temporarily store the powder and remove it to the outside. Also, the powder may be temporarily piled up on the ground without using such a powder storage facility, in which case the ground becomes the powder destination Z.
また前記実施形態では、ハウジング1の上壁1t(従ってホッパHの上端部)に着脱可能な分離機本体31として直方体状の中空ボックス体で構成したものを例示したが、本発明の分離機本体は、その内部で少なくとも粉粒体とエアとを分離してホッパHの開放上面に投入可能な構造であればよく、例えば従来周知のサイクロン式分離機のように円筒状の分離機本体を有した分離機構造であってもよい。 In the above embodiment, the separator body 31 is detachably attached to the upper wall 1t of the housing 1 (and therefore to the upper end of the hopper H) and is configured as a rectangular hollow box body. However, the separator body of the present invention may have any structure that can separate at least the powder and granular material and the air therein and feed them onto the open top surface of the hopper H. For example, the separator may have a cylindrical separator body like a conventionally known cyclone separator.
また前記実施形態では、分離機本体31内に仕切り板やフィルタが設けられない例を示したが、本発明では、投入口Toから投入される粉粒体とエアとを分離し易くするために、分離機本体31内に、投入口Toと排気口Do間のエア流通は許容する仕切り板やフィルタを配設してもよい。 In the above embodiment, an example was shown in which no partition plate or filter was provided inside the separator body 31. However, in the present invention, in order to facilitate separation of the powder and granular material fed from the feed port To and the air, a partition plate or filter that allows air to flow between the feed port To and the exhaust port Do may be provided inside the separator body 31.
また前記実施形態では、投入管Tの投入口Toを分離室33内に開口させて、その投入口Toより分離室33を経てホッパH内に粉粒体が投入されるものを示したが、本発明では、投入管Tの、投入口Toが開口した内端を実施形態の構造より下方に延ばして、投入口ToをホッパH内に直接開口させることで、投入口ToからホッパH内に粉粒体を投入してもよい。 In the above embodiment, the inlet To of the feed tube T is opened into the separation chamber 33, and the powdered material is fed from the inlet To into the hopper H through the separation chamber 33. However, in the present invention, the inner end of the feed tube T where the inlet To is open may be extended downward from the structure of the embodiment, and the inlet To may be opened directly into the hopper H, so that the powdered material may be fed into the hopper H from the inlet To.
また前記実施形態では、ホッパHの上端部が固定される、エア搬送装置Aのハウジング1(具体的には上壁1t)に分離機本体31を着脱可能に結合して、そのハウジング1を介して分離機本体31をホッパHの上端部に結合したものを示したが、本発明では、分離機本体31をホッパHの上端部に着脱可能に直接、結合してもよい。 In the above embodiment, the separator body 31 is removably connected to the housing 1 (specifically, the upper wall 1t) of the air conveying device A to which the upper end of the hopper H is fixed, and the separator body 31 is connected to the upper end of the hopper H via the housing 1. However, in the present invention, the separator body 31 may be directly and removably connected to the upper end of the hopper H.
また前記実施形態では、導入管Iを通して外部の粉粒体貯留部Cより投入管T側に粉粒体を流動させるエア流を発生可能な「エア流発生装置」として、排気管Dを通して分離室33内のエアを吸引して外部に排出可能な吸引ブロワ36を主要部とする吸引排気装置ADを例示したが、本発明のエア流発生装置は、実施形態のように排気管D側に配設しないで、導入管I側に配設してもよい。この場合、図示はしないが、例えば、導入管Iの途中に、導入管I内に投入管T側に向かうエア流を発生させるブロワを直列に介設し、このブロワ内に、粉粒体貯留部Cからの粉粒体及びエアを一緒に流動させるようにしてもよい。或いはまた、導入管Iの途中に、粉粒体貯留部Cから投入管T側に向かうエア流を導入管I内に発生させるブロワと、そのブロワの吸引力を利用して粉粒体貯留部Cから導入管I内に吸引した粉粒体及びエアを分離し且つ粉粒体を投入管T側に誘導するサイクロン式分離機とを互いに並列に介設してもよい。 In the above embodiment, the suction and exhaust device AD, whose main component is a suction blower 36 capable of sucking air from the separation chamber 33 through the exhaust pipe D and discharging it to the outside, is exemplified as an "air flow generating device" capable of generating an air flow that causes the powder to flow from the external powder storage section C to the input pipe T through the input pipe I, but the air flow generating device of the present invention may be disposed on the input pipe I side, rather than on the exhaust pipe D side as in the embodiment. In this case, although not shown, for example, a blower that generates an air flow in the input pipe I toward the input pipe T side may be disposed in series in the middle of the input pipe I, and the powder and air from the powder storage section C may be caused to flow together in this blower. Alternatively, a blower that generates an air flow from the powder/granular material storage section C toward the input tube T in the input tube I and a cyclone separator that uses the suction force of the blower to separate the powder/granular material and air sucked into the input tube I from the powder/granular material storage section C and guide the powder/granular material to the input tube T may be installed in parallel in the middle of the input tube I.
また特にエア流発生装置のブロワを上記の如く導入管Iに介設する場合には、前記実施形態のように排気管Dに吸引ブロワ36を設ける必要はなくなるが、排気管Dから外気に排気されるエア中に混じる粉塵や少量の粉粒体が周囲に飛散しないよう、前記実施形態と同様の集塵フィルタ37を排気管Dの大気開放口に接続しておくことが望ましい。 In particular, when the blower of the air flow generating device is inserted into the inlet pipe I as described above, there is no need to provide a suction blower 36 in the exhaust pipe D as in the previous embodiment. However, it is desirable to connect a dust collection filter 37 similar to that in the previous embodiment to the atmospheric opening of the exhaust pipe D to prevent dust particles and small amounts of powder mixed in the air exhausted from the exhaust pipe D from scattering into the surrounding area.
A・・・・・・粉粒体用エア搬送装置
AD・・・・・エア流発生装置としての吸引排気装置
C・・・・・・外部の粉粒体貯留部としてのコンテナ
D・・・・・・排気管
Do・・・・・排気口
H・・・・・・ホッパ
I・・・・・・導入管
M・・・・・・混相器
R・・・・・・ロータリバルブ
T・・・・・・投入管
To・・・・・投入口
Z・・・・・・粉粒体搬送先
3・・・・・・ブロワとしての搬送用ブロワ
4・・・・・・出口管
31・・・・・分離機本体
33・・・・・分離室
36・・・・・吸引ブロワ
Description of the Related Art A...Air conveying device for powder and granular material AD...Suction and exhaust device as an air flow generating device C...Container as an external powder and granular material storage section D...Exhaust pipe Do...Exhaust port H...Hopper I...Introducing pipe M...Mixer R...Rotary valve T...Feeding pipe To...Feeding port Z...Powder and granular material conveying destination 3...Conveying blower as a blower 4...Outlet pipe 31...Separator body 33...Separation chamber 36...Suction blower
Claims (3)
前記ホッパ(H)内に直接連通する分離室(33)を内部に有する中空の分離機本体(31)と、前記分離室(33)又は前記ホッパ(H)内に開口し且つ該ホッパ(H)内に粉粒体を投入可能な投入口(To)を一端に有して、前記分離機本体(31)に設けられる投入管(T)と、前記投入口(To)から投入された粉粒体の流入を抑制可能として前記分離室(33)に開口する排気口(Do)を有して、前記分離機本体(31)に設けられる排気管(D)と、前記投入管(T)の他端に接続されて外部の粉粒体貯留部(C)より粉粒体を該投入管(T)に導入可能な導入管(I)と、その導入管(I)を通して前記外部の粉粒体貯留部(C)より前記投入管(T)側に粉粒体を流動させるエア流を発生可能なエア流発生装置(AD)とを備え、
前記分離機本体(31)は、前記ホッパ(H)の上端部に着脱可能に結合されることを特徴とする、粉粒体用エア搬送装置。 The air conveying device for powdered or granular material includes a hopper (H) capable of charging and storing powdered or granular material, a rotary valve (R) connected to the lower part of the hopper (H) and forcibly discharging the powdered or granular material in the hopper (H), a blower (3) capable of ejecting air for pressurizing the powdered or granular material, and a phase mixer (M) that merges the air ejected from the blower (3) with the powdered or granular material discharged from the rotary valve (R) and directs the air toward an outlet pipe (4), and the ejected air is used to air convey the powdered or granular material from the outlet pipe (4) to a powdered or granular material conveying destination (Z) connected to the outlet pipe (4),
the separator body (31) is provided with a hollow separator body (31) having therein a separation chamber (33) directly communicating with the inside of the hopper (H); an input pipe (T) provided in the separator body (31) having at one end an input port (To) that opens into the separation chamber (33) or the hopper (H) and through which powder or granular material can be input into the hopper (H); an exhaust pipe (D) provided in the separator body (31) having an exhaust port (Do) that can suppress the inflow of the powder or granular material input from the input port (To) and opens into the separation chamber (33); an introduction pipe (I) connected to the other end of the input pipe (T) and capable of introducing powder or granular material from an external powder or granular material storage section (C) into the input pipe (T); and an air flow generating device (AD) capable of generating an air flow that causes the powder or granular material to flow from the external powder or granular material storage section (C) to the input pipe (T) through the introduction pipe (I);
The separator body (31) is detachably connected to the upper end of the hopper (H).
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