Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP7307920B2 - Dust collector, dust collector, solid preparation manufacturing device, dust collection system, and solid preparation manufacturing method - Google Patents
[go: Go Back, main page]

JP7307920B2 - Dust collector, dust collector, solid preparation manufacturing device, dust collection system, and solid preparation manufacturing method - Google Patents

Dust collector, dust collector, solid preparation manufacturing device, dust collection system, and solid preparation manufacturing method Download PDF

Info

Publication number
JP7307920B2
JP7307920B2 JP2019177541A JP2019177541A JP7307920B2 JP 7307920 B2 JP7307920 B2 JP 7307920B2 JP 2019177541 A JP2019177541 A JP 2019177541A JP 2019177541 A JP2019177541 A JP 2019177541A JP 7307920 B2 JP7307920 B2 JP 7307920B2
Authority
JP
Japan
Prior art keywords
suction port
dust
annular
cylindrical portion
granular material
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
JP2019177541A
Other languages
Japanese (ja)
Other versions
JP2020055642A (en
Inventor
悟史 今津
香織 渡部
祥吾 松永
善則 本多
耕士 北野
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Takasago Thermal Engineering Co Ltd
Cambridge Filter Corp
Original Assignee
Takasago Thermal Engineering Co Ltd
Cambridge Filter Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Takasago Thermal Engineering Co Ltd, Cambridge Filter Corp filed Critical Takasago Thermal Engineering Co Ltd
Publication of JP2020055642A publication Critical patent/JP2020055642A/en
Application granted granted Critical
Publication of JP7307920B2 publication Critical patent/JP7307920B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Basic Packing Technique (AREA)
  • Medical Preparation Storing Or Oral Administration Devices (AREA)

Description

本開示は、集塵用器具、集塵装置、固形製剤製造装置、集塵システム、及び固形製剤製造方法に関する。 TECHNICAL FIELD The present disclosure relates to a dust collection device, a dust collector, a solid formulation manufacturing apparatus, a dust collection system, and a solid formulation manufacturing method.

機械上部の投入口から材料(粉粒体)を投入し、分包した製品を製造する固形製剤充填機が知られている。この充填機のように投入口に粉粒体を投入する装置では、粉粒体投入時に投入口の周囲に粉塵が飛散することの防止対策として、例えば投入口の上方に排気フードを設置して、飛散した粉塵を排気フードから吸い出すことが行われる(例えば特許文献1)。 BACKGROUND ART A solid formulation filling machine is known in which a material (powder or granular material) is introduced from an inlet on the top of the machine to produce divided products. In a device such as this filling machine that feeds powder into the inlet, an exhaust hood is installed above the inlet as a measure to prevent dust from scattering around the inlet when the powder is fed. , the scattered dust is sucked out from an exhaust hood (for example, Patent Document 1).

特開2009-249359号公報JP 2009-249359 A

しかし、排気フードでは、吸い込んだ粉塵が完全に排出されずに一部がフード内周面に付着して残る場合がある。この場合、フードの清掃が充分でないと、後に付着した粉塵の塊が脱離・落下し製品へ混入の虞がある。 However, in the exhaust hood, the sucked dust may not be completely discharged and part of the dust may remain attached to the inner peripheral surface of the hood. In this case, if the hood is not sufficiently cleaned, clumps of dust that have adhered later may come off and fall off and be mixed into the product.

本開示は、粉粒体投入時の粉塵発生をより効率よく、かつ効果高く抑制できる集塵用器具、集塵装置、固形製剤製造装置、集塵システム、及び固形製剤製造方法を提供することを目的とする。 The present disclosure aims to provide a dust collecting device, a dust collector, a solid preparation manufacturing apparatus, a dust collection system, and a solid preparation manufacturing method that can more efficiently and effectively suppress the generation of dust when powdered or granular material is introduced. aim.

本発明の実施形態の一観点に係る集塵用器具は、粉粒体が投入される装置の投入口に設置される集塵用器具であって、前記粉粒体が通過する筒状部と、前記筒状部の外周側に設けられる環状管路と、前記筒状部の内周面の周方向全体に亘って設けられ、前記筒状部の内側と前記環状管路との間を連通して、粉粒体投入に伴い発生する粉塵を前記環状管路に吸入する吸入口と、前記環状管路の一端に設けられ外部と連通し、前記環状管路に吸引した前記粉塵を外部に吸い出すための吸出口と、を備え、前記環状管路は、前記吸出口が設けられる前記一端から他端に進むほど断面積が小さくなるよう形成されるA dust collecting device according to an aspect of an embodiment of the present invention is a dust collecting device installed at an inlet of a device into which powdery or granular material is introduced, comprising: a cylindrical portion through which the powdery or granular material passes; and an annular pipeline provided on the outer peripheral side of the tubular portion, and an annular pipeline provided along the entire circumferential direction of the inner peripheral surface of the tubular portion to communicate between the inner side of the tubular portion and the annular pipeline. and a suction port provided at one end of the annular conduit for inhaling dust generated by charging the granular material into the annular conduit and communicating with the outside to discharge the dust sucked into the annular conduit to the outside. and a suction port for sucking out the liquid, and the annular conduit is formed so that the cross-sectional area decreases as it progresses from the one end where the suction port is provided to the other end.

同様に、本発明の実施形態の一観点に係る集塵装置は、上記の集塵用器具と、前記集塵用器具の前記吸出口に接続され、前記環状管路内の空気を吸い出す空気吸出し装置と、を有する。 Similarly, a dust collector according to an aspect of an embodiment of the present invention includes the above-described dust collecting device, and an air suction device connected to the suction port of the dust collecting device to suck air in the annular conduit. and an apparatus.

同様に、本発明の実施形態の一観点に係る固形製剤製造装置は、投入口に投入される粉粒体を袋体に充填して固形製剤を出力する固形製剤製造装置であって、上記の集塵用器具が前記投入口に設置される。 Similarly, a solid preparation manufacturing apparatus according to one aspect of an embodiment of the present invention is a solid preparation manufacturing apparatus that outputs a solid preparation by filling a bag with powder or granular material to be fed into an inlet, wherein A dust collector is installed in the inlet.

同様に、本発明の実施形態の一観点に係る集塵システムは、投入口に投入される粉粒体を袋体に充填して出力する充填装置と、前記投入口に前記集塵用器具が設置された上記の集塵装置と、を備える。 Similarly, a dust collection system according to an aspect of an embodiment of the present invention includes a filling device that fills a bag with powder or granular material that is put into an inlet and outputs the bag, and the dust collection device that is placed in the inlet. and the dust collector installed above.

同様に、本発明の実施形態の一観点に係る固形製剤製造方法は、粉粒体が通過する筒状部と、前記筒状部の外周側に設けられる環状管路と、前記筒状部の内周面の周方向全体に亘って設けられ、前記筒状部の内側と前記環状管路との間を連通して、粉粒体投入に伴い発生する粉塵を前記環状管路に吸入する吸入口と、前記環状管路の一端に設けられ外部と連通し、前記環状管路に吸引した前記粉塵を外部に吸い出すための吸出口と、を備え、前記環状管路は、前記吸出口が設けられる前記一端から他端に進むほど断面積が小さくなるよう形成される、集塵用器具を、前記粉粒体が投入される装置の投入口に設置するステップと、前記集塵用器具の前記吸出口に空気吸出し装置を接続して、前記環状管路内の空気を吸い出すステップと、前記投入口に投入される前記粉粒体を袋体に充填して固形製剤を出力するステップと、を含む。

Similarly, the method for producing a solid preparation according to one aspect of the embodiment of the present invention includes a cylindrical portion through which the powder or granular material passes, an annular pipeline provided on the outer peripheral side of the cylindrical portion, and the cylindrical portion. A suction unit provided along the entire circumferential direction of the inner peripheral surface, communicating between the inside of the cylindrical portion and the annular pipeline, and sucking dust generated along with the introduction of powder or granular material into the annular pipeline. and a suction port provided at one end of the annular pipeline and communicating with the outside for sucking out the dust sucked into the annular pipeline , wherein the annular pipeline is provided with the suction port. a step of installing a dust collecting device formed so that the cross-sectional area becomes smaller as it progresses from the one end to the other end of the dust collecting device at the inlet of the device into which the granular material is charged; connecting an air suction device to the suction port to suck out the air in the annular pipeline; include.

本開示によれば、粉粒体投入時の粉塵発生をより効率よく、かつ効果高く抑制できる集塵用器具、集塵装置、固形製剤製造装置、及び集塵システム、及び固形製剤製造方法を提供することができる。 According to the present disclosure, a dust collection device, a dust collector, a solid preparation production apparatus, a dust collection system, and a solid preparation production method that can more efficiently and effectively suppress the generation of dust when powders are added are provided. can do.

実施形態に係る集塵システムを示す模式図である。It is a mimetic diagram showing a dust collection system concerning an embodiment. 実施形態に係る集塵用器具の組立斜視図である。It is an assembly perspective view of the instrument for dust collection which concerns on embodiment. 実施形態に係る集塵用器具の分解斜視図である。1 is an exploded perspective view of a dust collecting device according to an embodiment; FIG. 図2中のIV-IV断面図である。FIG. 3 is a sectional view along IV-IV in FIG. 2; 上部本体の上面図である。Fig. 10 is a top view of the upper body; 環状管路の空気の流れを示す模式図である。FIG. 4 is a schematic diagram showing the flow of air in an annular conduit; 筒状部の内周面に設けられる吸入口の配置パターンの一例を示す図である。FIG. 4 is a diagram showing an example of an arrangement pattern of suction ports provided on an inner peripheral surface of a cylindrical portion;

以下、添付図面を参照しながら実施形態について説明する。説明の理解を容易にするため、各図面において同一の構成要素に対しては可能な限り同一の符号を付して、重複する説明は省略する。 Embodiments will be described below with reference to the accompanying drawings. In order to facilitate understanding of the description, the same constituent elements in each drawing are denoted by the same reference numerals as much as possible, and overlapping descriptions are omitted.

なお、各図面において、x方向、y方向、z方向は互いに直交する方向である。典型的にはx方向及びy方向が水平方向であり、z方向は鉛直方向である。x方向は吸出口51の軸線方向である。z方向は、集塵用器具4の上部部材41及び下部部材42の積層方向である。以下の説明では、z正方向側を「上側」、z負方向側を「下側」とも表記する。 In each drawing, the x-direction, the y-direction, and the z-direction are directions orthogonal to each other. Typically the x and y directions are horizontal and the z direction is vertical. The x direction is the axial direction of the suction port 51 . The z direction is the stacking direction of the upper member 41 and the lower member 42 of the dust collecting device 4 . In the following description, the positive z direction side is also referred to as the "upper side" and the negative z direction side is referred to as the "lower side".

<集塵システム>
まず図1を参照して、本実施形態に係る集塵用器具4が適用される集塵システム1について説明する。図1は、実施形態に係る集塵システム1を示す模式図である。
<Dust collection system>
First, with reference to FIG. 1, a dust collection system 1 to which a dust collection device 4 according to this embodiment is applied will be described. FIG. 1 is a schematic diagram showing a dust collection system 1 according to an embodiment.

図1に示すように、集塵システム1は、充填装置2と、集塵装置3とを含む。充填装置2は、投入口21に投入された粉粒体24を袋体25に充填して出力する装置である。充填装置2は、典型的には、上方に開口する投入口21へ粉粒体24を投入して、カプセルや小袋などの袋体25に充填して分包された製品を生成する。充填装置2は、例えば投入口21に投入された粉粒体24がホッパ21aで集約されて本体22に導入され、本体22の内部にてカプセルや小袋などの袋体25に充填され出力部23から出力される。 As shown in FIG. 1 , the dust collection system 1 includes a filling device 2 and a dust collector 3 . The filling device 2 is a device that fills a bag 25 with the granular material 24 introduced into the inlet 21 and outputs the same. The filling device 2 typically injects the granular material 24 into an inlet 21 that opens upward, and fills a bag 25 such as a capsule or a small bag with the powder to produce a packaged product. In the filling device 2, for example, powdery grains 24 fed into an inlet 21 are aggregated by a hopper 21a and introduced into a main body 22. Inside the main body 22, a bag 25 such as a capsule or a small bag is filled, and an output section 23 is filled. output from

なお、本実施形態の充填装置2は、投入口21に投入される粉粒体を袋体25に充填して固形製剤を出力する「固形製剤製造装置」も包含する。 The filling device 2 of the present embodiment also includes a “solid preparation manufacturing device” that fills the bag body 25 with powder or granular material that is introduced into the inlet 21 and outputs a solid preparation.

充填装置2の投入口21に粉粒体24が投入される際には、粉粒体24がホッパ21aや投入口21の内壁にぶつかるなどの原因により、投入口21から外部に粉塵が発生する場合がある。集塵装置3は、このように充填装置2の投入口21に発生する粉塵を収集するための装置である。集塵装置3は、集塵用器具4と、空気吸出し装置5と、空気供給装置6とを備える。 When the granular material 24 is introduced into the charging port 21 of the filling device 2, dust is generated outside from the charging port 21 because the granular material 24 collides with the hopper 21a and the inner wall of the charging port 21. Sometimes. The dust collector 3 is a device for collecting dust generated at the inlet 21 of the filling device 2 in this way. The dust collector 3 includes a dust collector 4 , an air suction device 5 and an air supply device 6 .

集塵用器具4は、充填装置2の投入口21に設置される。集塵用器具4は、典型的には投入口21の上端の外縁に沿って嵌め付けられる。投入口21の上方に設置された集塵用器具4は、充填装置2に投入された粉粒体24を投入口21の代わりに受け、発生した粉塵を空気吸出し装置5に誘導する。集塵用器具4の詳細については後述する。 The dust collecting device 4 is installed at the inlet 21 of the filling device 2 . The dust collecting device 4 is typically fitted along the outer edge of the upper end of the inlet 21 . The dust collector 4 installed above the inlet 21 receives the powder 24 introduced into the filling device 2 instead of the inlet 21 and guides the generated dust to the air suction device 5 . Details of the dust collecting device 4 will be described later.

空気吸出し装置5は、集塵用器具4の吸出口51に接続され、集塵用器具4の内部の環状管路48(図4参照)から空気を吸い出すことにより粉塵を収集する。空気吸出し装置5は、吸引装置5aと、チューブ5bとを有する。チューブ5bは吸出口51と吸引装置5aとの間を連通可能に接続する。吸引装置5aはチューブ5bを介して集塵用器具4に吸引力を伝達して、集塵用器具4から粉塵を吸い出すことができる。 The air suction device 5 is connected to the suction port 51 of the dust collecting device 4 and collects dust by sucking air from an annular pipe 48 (see FIG. 4) inside the dust collecting device 4 . The air suction device 5 has a suction device 5a and a tube 5b. The tube 5b communicably connects the suction port 51 and the suction device 5a. The suction device 5a can transmit suction force to the dust collecting device 4 via the tube 5b to suck out the dust from the dust collecting device 4. As shown in FIG.

空気供給装置6は、集塵用器具4より粉粒体24の投入側(上側)に設けられ、フィルタ装置62により洗浄された洗浄空気を集塵用器具4の方向へ送出する。空気供給装置6は、ファン61とフィルタ装置62とを有する。フィルタ装置62の上方にファン61が配置され、ファン61は回転駆動すると鉛直下方の集塵用器具4の投入口21に向かって風を発生させる。ファン61により発生した風はフィルタ装置62を通過して洗浄されて、空気供給装置6からは洗浄空気が出力される。 The air supply device 6 is provided on the input side (upper side) of the particulate matter 24 from the dust collecting device 4 and feeds the cleaning air washed by the filter device 62 toward the dust collecting device 4 . The air supply device 6 has a fan 61 and a filter device 62 . A fan 61 is arranged above the filter device 62, and when the fan 61 is rotationally driven, it generates a wind toward the inlet 21 of the dust collecting device 4 vertically downward. The air generated by the fan 61 passes through the filter device 62 and is cleaned, and the cleaning air is output from the air supply device 6 .

このように集塵装置3は、充填装置2の投入口21に発生する粉塵の抑制のために2つの要素を備える。第1の要素は、集塵用器具4と空気吸出し装置5との組み合わせであり、集塵用器具4で効率良く粉塵を収集して、空気吸出し装置5で回収することにより、粉塵発生を抑制する。第2の要素は空気供給装置6であり、投入口21へ洗浄空気を供給して粉塵が上方舞い上がるのを防止することにより、粉塵発生を抑制する。集塵装置3は、これらの2つの要素を併用することにより、粉塵発生の抑制を効率よく、かつ効果高く行うことができる。 Thus, the dust collector 3 has two elements for suppressing dust generated at the inlet 21 of the filling device 2 . The first element is a combination of the dust collection device 4 and the air suction device 5. By efficiently collecting dust with the dust collection device 4 and collecting it with the air suction device 5, dust generation is suppressed. do. The second element is the air supply device 6, which supplies cleansing air to the input port 21 to prevent the dust from rising upwards, thereby suppressing the generation of dust. By using these two elements together, the dust collector 3 can efficiently and effectively suppress the generation of dust.

なお、集塵装置3は、空気供給装置6を含まず、集塵用器具4と空気吸出し装置5との組み合わせのみを備える構成でもよい。 Note that the dust collector 3 may be configured to include only a combination of the dust collector 4 and the air suction device 5 without including the air supply device 6 .

集塵装置3の集塵用器具4は、図1に示した充填装置2の投入口21に取り付ける独立した物体ではなく、充填装置2の投入口21に一体的にその機能が含まれる構成でもよい。この場合、例えば投入口21の内壁に後述する吸入口49(図4参照)が設けられ、内壁の周囲に環状管路48が設けられる。また、投入口21の外壁に吸出口51が設けられる。 The dust collecting device 4 of the dust collector 3 is not an independent object attached to the inlet 21 of the filling device 2 shown in FIG. good. In this case, for example, a suction port 49 (see FIG. 4), which will be described later, is provided on the inner wall of the inlet 21, and an annular conduit 48 is provided around the inner wall. A suction port 51 is provided on the outer wall of the inlet 21 .

<集塵用器具>
図2~図7を参照して、本実施形態に係る集塵用器具4の構成を説明する。図2は、実施形態に係る集塵用器具4の組立斜視図である。図3は、実施形態に係る集塵用器具4の分解斜視図である。図4は、図2中のIV-IV断面図である。図5は、上部本体43の上面図である。図6は、環状管路48の空気の流れを示す模式図である。図7は、筒状部47の内周面に設けられる吸入口49の配置パターンの一例を示す図である。
<Dust collection device>
The configuration of the dust collecting device 4 according to the present embodiment will be described with reference to FIGS. 2 to 7. FIG. FIG. 2 is an assembled perspective view of the dust collecting device 4 according to the embodiment. FIG. 3 is an exploded perspective view of the dust collecting device 4 according to the embodiment. FIG. 4 is a sectional view taken along line IV-IV in FIG. 5 is a top view of the upper body 43. FIG. FIG. 6 is a schematic diagram showing the flow of air in the annular conduit 48. As shown in FIG. FIG. 7 is a diagram showing an example of an arrangement pattern of the suction ports 49 provided on the inner peripheral surface of the cylindrical portion 47. As shown in FIG.

図2、図3に示すように、集塵用器具4は、上部部材41(第1部材)と下部部材42(第2部材)の2つの部材が上下に積載されて構成される。上部部材41は、上部本体43と、上板44と、蓋45とを有する。上部本体43の上側から上板44が取り付けられ、上板44の上側から蓋45が取り付けられる。下部部材42は、じょうご部46と、連結部57とを有する。連結部57の上方にじょうご部46が配置される。 As shown in FIGS. 2 and 3, the dust collecting device 4 is constructed by vertically stacking two members, an upper member 41 (first member) and a lower member 42 (second member). The upper member 41 has an upper body 43 , a top plate 44 and a lid 45 . A top plate 44 is attached from above the upper body 43 , and a lid 45 is attached from above the top plate 44 . The lower member 42 has a funnel portion 46 and a connecting portion 57 . The funnel portion 46 is arranged above the connecting portion 57 .

上部本体43は、粉粒体24が通過する筒状部47と、筒状部47の外周側に設けられる筐体50とを備える。筒状部47を形成する内壁と、筐体50の外壁とで、筒状部47の外周側に設けられる環状管路48が形成されている。図2、図5、図6に示すように、筒状部47及び環状管路48は円環形状である。環状管路48の下端は、筒状部47と筐体50との間に亘って設けられる底板56で封止されている。一方、環状管路48の上端は、図4に示すように脱着可能な上板44で塞がれている。メンテナンス時には上板44を上部本体43から取り外すことにより、環状管路48の上面を流れ方向の全体に亘って開口させることができ、管路内を容易に清掃できるよう構成されている。 The upper main body 43 includes a tubular portion 47 through which the granular material 24 passes, and a housing 50 provided on the outer peripheral side of the tubular portion 47 . An inner wall forming the tubular portion 47 and an outer wall of the housing 50 form an annular pipe 48 provided on the outer peripheral side of the tubular portion 47 . As shown in FIGS. 2, 5 and 6, the tubular portion 47 and the annular conduit 48 are annular. The lower end of the annular conduit 48 is sealed with a bottom plate 56 provided between the tubular portion 47 and the housing 50 . On the other hand, the upper end of the annular conduit 48 is closed with a detachable upper plate 44 as shown in FIG. By removing the upper plate 44 from the upper body 43 during maintenance, the upper surface of the annular conduit 48 can be opened over the entire flow direction, and the inside of the conduit can be easily cleaned.

図3、図5に示すように、環状管路48の上端には、筒状部47の周方向に沿った略90°間隔で、筒状部47と筐体50とを連結する補強板53が設けられる。補強板53は、主面が上下方向、長手方向が筒状部47の径方向となるよう配置され、長手方向の一端が筒状部47に接続され、他端が筐体50と接続されている。補強板53は、環状管路48の幅を保持すると共に、上板44の底面を支持する。 As shown in FIGS. 3 and 5 , reinforcing plates 53 are provided on the upper end of the annular conduit 48 to connect the tubular portion 47 and the housing 50 at approximately 90° intervals along the circumferential direction of the tubular portion 47 . is provided. The reinforcing plate 53 is arranged so that its main surface is in the vertical direction and its longitudinal direction is in the radial direction of the cylindrical portion 47 , and one end in the longitudinal direction is connected to the cylindrical portion 47 and the other end is connected to the housing 50 . there is The reinforcing plate 53 maintains the width of the annular pipeline 48 and supports the bottom surface of the upper plate 44 .

上板44は、上部本体43の上端と略同一形状であり、上部本体43の上端に取り付けられる。また、上板44の中央部分には略円形状の開口44aが設けられる。開口44aは、z方向から視たときに筒状部47と重複する位置に設けられ、上板44が上部本体43に組み付けられたときに、環状管路48を塞ぎ、かつ、筒状部47が外部に開口するように形成されている。また、蓋45は上板44の開口44aを塞ぐように上板44に取り付けられる。蓋45が取り付けられた状態では、筒状部47は上端の開口が塞がれる。例えば充填装置2の非使用時に上板44の開口44aを蓋45で塞ぐことで、ゴミなどの不純物が充填装置2の投入口21に落下・浸入するのを防止できる。 The upper plate 44 has substantially the same shape as the upper end of the upper body 43 and is attached to the upper end of the upper body 43 . A substantially circular opening 44 a is provided in the central portion of the upper plate 44 . The opening 44a is provided at a position overlapping the tubular portion 47 when viewed in the z-direction, and when the upper plate 44 is assembled to the upper body 43, the opening 44a closes the annular conduit 48 and closes the tubular portion 47. is formed to open to the outside. Also, the lid 45 is attached to the upper plate 44 so as to close the opening 44a of the upper plate 44 . When the lid 45 is attached, the opening at the upper end of the cylindrical portion 47 is closed. For example, by covering the opening 44a of the upper plate 44 with the lid 45 when the filling device 2 is not in use, it is possible to prevent impurities such as dust from falling into and entering the inlet 21 of the filling device 2. FIG.

図5、図6に示すように、筒状部47と筐体50との間に2枚の仕切り板52、55が配置され、環状管路48を塞いでいる。仕切り板55は、筒状部47の円形状のx正方向側の略中央位置に、筒状部47の径方向に沿って延在するよう配置されている。仕切り板52は、仕切り板55よりy正方向側の位置に配置されている。吸出口51は、仕切り板55よりy負方向側の位置に設けられる。図6は、図5から環状管路48を強調表示した模式図であり、図中の網掛け部分が環状管路48を示す。図6に示すように、環状管路48は、仕切り板52側の端部48A(他端)から始まり、筒状部47に沿って反時計回りに仕切り板55側の端部48B(一端)まで延在する。吸出口51は、環状管路48の一端側の端部48Bに設けられる。 As shown in FIGS. 5 and 6 , two partition plates 52 and 55 are arranged between the tubular portion 47 and the housing 50 to block the annular conduit 48 . The partition plate 55 is arranged so as to extend along the radial direction of the tubular portion 47 at a substantially central position on the positive x direction side of the circular tubular portion 47 . The partition plate 52 is arranged at a position on the positive y direction side of the partition plate 55 . The suction port 51 is provided at a position on the y negative direction side of the partition plate 55 . FIG. 6 is a schematic diagram highlighting the annular pipeline 48 from FIG. As shown in FIG. 6, the annular conduit 48 starts from an end 48A (the other end) on the side of the partition plate 52 and extends counterclockwise along the tubular portion 47 to an end 48B (the one end) on the side of the partition plate 55. extends up to The suction port 51 is provided at the end portion 48B on the one end side of the annular conduit 48 .

z方向から視た場合、仕切り板52は仕切り板55に対して、環状管路48の流れ方向に傾斜するよう配置されている。言い換えると、仕切り板52は内側の筒状部47と接触する端部より、外側の筐体50と接触する端部のほうが環状管路48の下流側(反時計回り方向)に配置されている。これにより、後述する吸入口49から環状管路48に導入された粉塵をスムーズに環状管路48の下流側に誘導することができる。 When viewed from the z-direction, the partition plate 52 is arranged so as to be inclined with respect to the partition plate 55 in the flow direction of the annular pipeline 48 . In other words, the end portion of the partition plate 52 that contacts the outer casing 50 is arranged downstream (counterclockwise direction) of the annular conduit 48 than the end portion that contacts the inner cylindrical portion 47 . . As a result, the dust introduced into the annular pipe 48 from the suction port 49 (to be described later) can be smoothly guided to the downstream side of the annular pipe 48 .

仕切り板52は、例えば筐体50と筒状部47との間に固定される。仕切り板55は、例えば上板44の底面からz負方向に突出して設けられ、上板44を上部本体43に取り付けるときに環状管路48に挿入される。なお、2枚の仕切り板52、55は、環状管路48の起端側と終端側とを区分できればよく、一方のみを設ける構成でもよい。 The partition plate 52 is fixed between the housing 50 and the cylindrical portion 47, for example. The partition plate 55 is provided, for example, so as to protrude from the bottom surface of the upper plate 44 in the z-negative direction, and is inserted into the annular conduit 48 when the upper plate 44 is attached to the upper body 43 . In addition, the two partition plates 52 and 55 only need to be able to separate the starting end side and the terminal end side of the annular pipeline 48, and only one of them may be provided.

図5に示すように、z方向から視た場合、吸出口51はその軸線Cの方向が筒状部47の円環形状の接線Bの方向と平行であり、かつ、筒状部47の中心からずれる位置に設けられる。接線Bは、筒状部47の円環形状のうち最もy負方向側の接点A(言い換えると、筒状部47の中心を通りy軸と平行は直線の交点A)を通る接線であり、x軸と平行である。つまり吸出口51の軸線Cもx軸と平行である。吸出口51は、筒状部47の中心からy負方向側へずれており、上記の接線Bが吸出口51内を通過できる位置に設けられている。吸出口51は、筐体50のy負方向側の側面より内側(y正方向側)にあるのが好ましい。 As shown in FIG. 5, when viewed from the z direction, the direction of the axis C of the suction port 51 is parallel to the direction of the tangent line B of the annular shape of the cylindrical portion 47, and the center of the cylindrical portion 47 provided at a position displaced from the The tangent line B is a tangent line that passes through the contact point A on the most negative y direction side of the annular shape of the cylindrical portion 47 (in other words, the intersection point A of a straight line that passes through the center of the cylindrical portion 47 and is parallel to the y axis), parallel to the x-axis. That is, the axis C of the suction port 51 is also parallel to the x-axis. The suction port 51 is offset from the center of the cylindrical portion 47 in the y negative direction, and is provided at a position where the tangent line B can pass through the suction port 51 . The suction port 51 is preferably located inside (y positive direction side) of the side surface of the housing 50 on the y negative direction side.

環状管路48は、粉粒体24の投入方向(z方向)から視たときに、筐体50のy方向の中央位置に対して筒状部47の軸心位置をy正方向側にずらすことにより、吸出口51が設けられる一端(端部48B)から他端(端部48A)に進むほど筒状部47の内壁と筐体50の外壁との距離が小さくなるよう形成される。これにより、環状管路48は、吸出口51が設けられる一端から他端に進むほど断面積が小さくなるよう形成される。 The annular conduit 48 shifts the axial center position of the cylindrical portion 47 in the positive y direction with respect to the central position of the housing 50 in the y direction when viewed from the direction (z direction) of the powdery material 24 being introduced. As a result, the distance between the inner wall of the tubular portion 47 and the outer wall of the housing 50 is formed to decrease from one end (end portion 48B) where the suction port 51 is provided to the other end (end portion 48A). Thereby, the annular pipeline 48 is formed such that the cross-sectional area decreases from one end where the suction port 51 is provided to the other end.

図3、図4に示すように、筒状部47の内周面には、内周面の周方向全体に亘って複数の吸入口49が設けられている。吸入口49は、筒状部47の内側と環状管路48との間を連通して、粉粒体24投入に伴い発生する粉塵を環状管路48に吸入する。 As shown in FIGS. 3 and 4, the inner peripheral surface of the tubular portion 47 is provided with a plurality of suction ports 49 along the entire inner peripheral surface. The suction port 49 communicates between the inner side of the tubular portion 47 and the annular conduit 48 and sucks dust generated along with the injection of the granular material 24 into the annular conduit 48 .

吸入口49は、配置される環状管路48の位置が、吸出口51が設けられる終端側の端部48B(一端)から起端側の端部48A(他端)に進むほど、吸入口49が設けられる内周面の面積に対する開口率が大きくなるよう形成される。例えば図7に示すように、環状管路48の起端側から終端側に沿って筒状部47を四分割して、最も起端側の第1領域47aでは吸入口49の開口率が40%、次の第2領域47bでは吸入口49の開口率が30%、次の第3領域47cでは吸入口49の開口率が20%、最も終端側の第4領域47dでは吸入口49の開口率が10%となるよう形成される。 The suction port 49 is arranged such that the position of the annular pipe line 48 arranged advances from the end portion 48B (one end) on the terminal side where the suction port 51 is provided to the end portion 48A (the other end) on the starting end side. is formed so that the aperture ratio with respect to the area of the inner peripheral surface provided with is large. For example, as shown in FIG. 7, the tubular portion 47 is divided into four along the end side from the starting end side of the annular conduit 48, and the opening ratio of the suction port 49 is 40 in the first region 47a on the most starting end side. %, the opening ratio of the suction port 49 is 30% in the next second region 47b, the opening ratio of the suction port 49 is 20% in the next third region 47c, and the opening of the suction port 49 is in the fourth region 47d on the most terminal side. Formed to have a rate of 10%.

開口率の増減は、図7に示すように各領域47a~47dで吸入口49の数は同数であり、各孔の大きさを変更することで調整できるが、他の手法でもよい。例えば、各領域47a~47dで吸入口49の大きさは同じにして、各領域47a~47dの吸入口49の数を変更することで開口率を調整してもよい。 The aperture ratio can be increased or decreased by changing the size of each hole since the number of suction ports 49 is the same in each region 47a to 47d as shown in FIG. 7, but another method may be used. For example, the opening ratio may be adjusted by making the size of the suction port 49 the same in each of the regions 47a to 47d and changing the number of the suction port 49 in each of the regions 47a to 47d.

また、吸入口49は、環状管路48の位置に応じて開口率を変動できればよく、吸入口49の形状は図7の円形以外の形状でもよい。例えば多角形状でもよいし、孔ではなくスリットでもよい。また、開口率の変動の幅は本実施形態の10~40%とは異なるものでもよいし、開口率の変動の段階は本実施形態の4段階とは異なるものでもよい。 Moreover, the suction port 49 only needs to be able to vary the opening ratio according to the position of the annular conduit 48, and the shape of the suction port 49 may be a shape other than the circular shape shown in FIG. For example, a polygonal shape may be used, and slits may be used instead of holes. Also, the range of variation in the aperture ratio may be different from 10 to 40% in this embodiment, and the steps of variation in the aperture ratio may be different from the four steps in this embodiment.

じょうご部46は、図3、図4に示すようにラッパ形状の筒状体であり、下部より上部の周長が長く上方に広がって形成されている。じょうご部46は、筒状部47と同様に中央に粉粒体24を通過させることができる。 As shown in FIGS. 3 and 4, the funnel portion 46 is a trumpet-shaped cylindrical body, and is formed such that the upper portion is longer in circumference than the lower portion and spreads upward. The funnel portion 46 can allow the granular material 24 to pass through the center similarly to the cylindrical portion 47 .

じょうご部46の下端には連結部57が接続される。連結部57は下方が開口している箱型の部材であり、略矩形状の天板57aと、天板57aの外縁に沿って下方に突出して設けられる枠体57bとを有する。天板57aにじょうご部46の下端が貫通しており、上方から投入された粉粒体24を下方に通過させることができる。連結部57は、図4に示すように枠体57bが充填装置2の投入口21の上部開口と同形状で形成され、投入口21の外側に枠体57bが嵌って、天板57aが投入口21の上端により支持されることによって、投入口21に取り付けられる。 A connecting portion 57 is connected to the lower end of the funnel portion 46 . The connecting portion 57 is a box-shaped member with an open bottom, and has a substantially rectangular top plate 57a and a frame body 57b protruding downward along the outer edge of the top plate 57a. The lower end of the funnel portion 46 penetrates the top plate 57a, so that the granular material 24 introduced from above can pass downward. As shown in FIG. 4, the connecting portion 57 has a frame 57b formed in the same shape as the upper opening of the inlet 21 of the filling device 2. It is attached to the input port 21 by being supported by the upper end of the port 21 .

また、図4、図5に示すように、z方向から視たときにじょうご部46と筒状部47とが重なる位置で、じょうご部46の上端で上部部材41の底板56を支持することで、上部部材41と下部部材42とが一体的に組まれる。 4 and 5, the upper end of the funnel portion 46 supports the bottom plate 56 of the upper member 41 at a position where the funnel portion 46 and the cylindrical portion 47 overlap when viewed from the z direction. , the upper member 41 and the lower member 42 are assembled integrally.

図4に示すように、筒状部47の内周面は、じょうご部46の上端(筒状部47側の端部)より中心側に突出しており、筒状部47とじょうご部46との間に環状管路48の底板56の一部が露出している。この底板56の一部は、筒状部47のじょうご部46側(下側)の端部と、じょうご部46の筒状部47側(上側)の端部とを接続する「接続部」とも表現できる。 As shown in FIG. 4 , the inner peripheral surface of the tubular portion 47 protrudes toward the center from the upper end of the funnel portion 46 (the end on the tubular portion 47 side), and the tubular portion 47 and the funnel portion 46 are separated from each other. A portion of the bottom plate 56 of the annular conduit 48 is exposed therebetween. A portion of the bottom plate 56 is also referred to as a “connecting portion” that connects the end portion of the cylindrical portion 47 on the funnel portion 46 side (lower side) and the end portion of the funnel portion 46 on the cylindrical portion 47 side (upper side). can be expressed.

図5に示すように、底板56のうち筒状部47とじょうご部46との間に露出する部分(図5に径方向の幅Dで示す部分)には、第2吸入口54が筒状部47の周方向全体に亘って設けられる。第2吸入口54は、図4に示すように、じょうご部46の内側と環状管路48との間を連通して設けられ、粉粒体24投入に伴い発生する粉塵を環状管路48に吸入することができる。 As shown in FIG. 5, the portion of the bottom plate 56 exposed between the tubular portion 47 and the funnel portion 46 (the portion indicated by the radial width D in FIG. 5) has a second suction port 54 formed in a tubular shape. It is provided over the entire circumferential direction of the portion 47 . As shown in FIG. 4, the second suction port 54 is provided so as to communicate between the inside of the funnel portion 46 and the annular pipeline 48, and directs the dust generated along with the injection of the granular material 24 into the annular pipeline 48. Can be inhaled.

第2吸入口54は、図5では、筒状部47の周方向に沿ったスリット形状で形成されるが、周方向の全域から粉塵を吸入できればよく、例えば周方向に沿って複数の孔を連設する構成などの他の形状でもよい。 The second suction port 54 is formed in a slit shape along the circumferential direction of the cylindrical portion 47 in FIG. Other shapes, such as a contiguous configuration, may also be used.

次に本実施形態の集塵用器具4の効果を説明する。集塵用器具4は、粉粒体24が通過する筒状部47と、筒状部47の外周側に設けられる環状管路48と、筒状部47の内周面の周方向全体に亘って設けられ、筒状部47の内側と環状管路48との間を連通して、粉粒体24投入に伴い発生する粉塵を環状管路48に吸入する吸入口49と、環状管路48の一端に設けられ外部と連通する吸出口51と、を備える。 Next, the effects of the dust collecting device 4 of this embodiment will be described. The dust collecting device 4 includes a cylindrical portion 47 through which the powdery particles 24 pass, an annular pipe line 48 provided on the outer peripheral side of the cylindrical portion 47, and the entire inner peripheral surface of the cylindrical portion 47 in the circumferential direction. a suction port 49 for sucking into the annular pipeline 48 the dust generated along with the injection of the granular material 24, and the annular pipeline 48; and a suction port 51 that is provided at one end of the and communicates with the outside.

この構成により、図6に網掛け部分で示すように、筒状部47の外側に一方向(図6では反時計回り方向)に空気が流れ、吸出口51から外部に排出される空気の流れを作る環状管路48が形成される。そして、筒状部47の周方向全体に亘って設けられる吸入口49によって、環状管路48の全長に沿って常に筒状部47の内部側から環状管路48へ空気が流入する。このような空気の流れをつくることによって、筒状部47に投入された粉粒体24から粉塵が発生した場合に、筒状部47の内部空間のどの位置で粉塵が発生しても確実に吸入口49から環状管路48へ粉塵を導入でき、環状管路48内に導入された粉塵は吸出口51から速やかに排出できる。したがって、粉粒体24投入時に発生する粉塵を非常に効率よく収集することが可能となり、粉粒体24投入時の粉塵発生をより効率よく、かつ効果高く抑制できる。 With this configuration, as shown by the shaded area in FIG. 6, air flows in one direction (counterclockwise direction in FIG. 6) outside the cylindrical portion 47, and the air flow is discharged to the outside from the suction port 51. An annular conduit 48 is formed which creates a . Air always flows into the annular conduit 48 from the inside of the tubular part 47 along the entire length of the annular conduit 48 through the suction port 49 provided along the entire circumferential direction of the tubular part 47 . By creating such an air flow, when dust is generated from the granular material 24 thrown into the cylindrical portion 47, the dust is reliably generated at any position in the internal space of the cylindrical portion 47. Dust can be introduced from the suction port 49 into the annular conduit 48 , and the dust introduced into the annular conduit 48 can be quickly discharged from the suction port 51 . Therefore, it becomes possible to collect the dust generated when the granular material 24 is charged very efficiently, and the generation of dust when the granular material 24 is charged can be suppressed more efficiently and effectively.

また、本実施形態では、筒状部47及び環状管路48が円環形状であり、吸出口51は、その軸線方向が筒状部47の円環形状の接線方向(図5に示す接線Bの延在方向)と平行であり、かつ、筒状部47の中心からずれる位置に設けられる。図6に点線で示すように、吸出口51aが筒状部47の中心にあると、環状管路48から吸出口51に入る部分で流れが屈曲するため、環状管路48内の空気流れの損失が大きく、また、流れが屈曲する部分では環状管路48に粉塵が堆積しやすい。これに対して本実施形態のように吸出口51が筒状部47の中心からずれた位置にあると、筒状部47の周囲の環状の空気流れから吸出口51への誘導の際に、空気流れの屈曲が少なく比較的低抵抗でスムーズに空気が流れるので、環状管路48内の空気流れのエネルギー損失を軽減してより効率良く粉塵を排出できると共に、粉塵が環状管路48内に堆積するのを抑制できる。 Further, in the present embodiment, the cylindrical portion 47 and the annular conduit 48 are annular, and the axial direction of the suction port 51 is the tangential direction of the annular shape of the cylindrical portion 47 (the tangential line B shown in FIG. 5). extending direction) and is provided at a position displaced from the center of the cylindrical portion 47 . As shown by the dotted line in FIG. 6, when the air outlet 51a is located at the center of the tubular portion 47, the flow bends at the portion entering the air outlet 51 from the annular conduit 48. The loss is large, and dust tends to accumulate in the annular pipe 48 at the portion where the flow bends. On the other hand, if the suction port 51 is at a position deviated from the center of the cylindrical portion 47 as in the present embodiment, when the annular air flow around the cylindrical portion 47 is guided to the suction port 51, Since the air flow is less bent and flows smoothly with relatively low resistance, the energy loss of the air flow in the annular conduit 48 is reduced, dust can be discharged more efficiently, and the dust can be discharged into the annular conduit 48. Deposition can be suppressed.

また、本実施形態では、環状管路48は、吸出口51が設けられる一端から他端に進むほど断面積が小さくなるよう形成される。つまり環状管路48の始点から終点に向けて断面積が大きくなる。具体的には、本実施形態では、粉粒体24の投入方向(z方向)から視たときに、筐体50の中心位置に対して筒状部47の軸心位置をずらすことにより、吸出口51が設けられる一端から他端に進むほど、筒状部47の内壁と筐体50の外壁との距離が小さくなるように環状管路48が形成される。つまり環状管路48の始点(端部48A)から終点(端部48B)に向けて筒状部47の内壁と筐体50の外壁との距離が大きくなる。 In addition, in the present embodiment, the annular pipeline 48 is formed so that the cross-sectional area becomes smaller as it progresses from one end where the suction port 51 is provided to the other end. In other words, the cross-sectional area increases from the starting point of the annular conduit 48 toward the terminal point. Specifically, in the present embodiment, when viewed from the charging direction (z direction) of the granular material 24, the axial center position of the tubular portion 47 is shifted with respect to the center position of the housing 50, whereby the suction is performed. The annular conduit 48 is formed such that the distance between the inner wall of the cylindrical portion 47 and the outer wall of the housing 50 becomes smaller as it progresses from one end where the outlet 51 is provided to the other end. That is, the distance between the inner wall of the cylindrical portion 47 and the outer wall of the housing 50 increases from the start point (end portion 48A) of the annular conduit 48 toward the end point (end portion 48B).

環状管路48の断面積が流れ方向に沿って全て同じ大きさの場合には、空気吸出し装置5が環状管路48の終点(端部48B)に接続されるため、環状管路48の流れ方向の各位置の吸入口49において環状管路48内へ導入される風量は、終点に近いほど大きく、始点(端部48A)に近いほど小さくなる傾向がある。これに対して本実施形態では、上述のように環状管路48の断面積が、始点側に進むほど小さく、終点側に進むほど大きくなるよう形成されているため、環状管路48の流れ方向の各位置において吸入口49を流れる風量を均一化でき、この結果、環状管路48の流れ方向の全体で、吸入口49からの粉塵の吸い込み量も均一化できる。 If the cross-sectional areas of the annular pipeline 48 are all the same size along the flow direction, the air suction device 5 is connected to the end point (end 48B) of the annular pipeline 48, so that the flow of the annular pipeline 48 The amount of air introduced into the annular duct 48 at the suction port 49 at each position in the direction tends to be larger nearer the end point and smaller nearer the starting point (end portion 48A). On the other hand, in the present embodiment, as described above, the cross-sectional area of the annular pipeline 48 is formed so as to decrease toward the start point side and increase toward the end point side. The amount of air flowing through the suction port 49 can be made uniform at each position of , and as a result, the amount of dust sucked from the suction port 49 can be made uniform throughout the flow direction of the annular pipe 48 .

また、筒状部47に設けられる吸入口49は周方向の全体に亘って設けられるので、仮に周方向の各位置で略同量の粉塵を吸入した場合には、環状管路48の上流から下流に進むほど粉塵の量が増加する。これに対して、本実施形態のように、環状管路48の上流側から下流側に進むにつれて、例えば筒状部47の内壁と筐体50の外壁との距離を大きくするなど、管路の断面積を大きくするように形成することによって、環状管路48の各位置において粉塵の量に応じた充分な空間を確保できるので、粉塵が管路に詰まる事態を防止でき、粉塵を下流側にスムーズに流れやすくできる。 In addition, since the suction port 49 provided in the cylindrical portion 47 is provided over the entire circumferential direction, if substantially the same amount of dust is sucked at each position in the circumferential direction, the air will be sucked from the upstream of the annular duct 48 . The amount of dust increases as it goes downstream. On the other hand, as in the present embodiment, the distance between the inner wall of the tubular portion 47 and the outer wall of the housing 50 is increased as the annular pipe 48 progresses from the upstream side to the downstream side. By forming the cross-sectional area to be large, a sufficient space corresponding to the amount of dust can be secured at each position of the annular pipe 48, so that the pipe can be prevented from being clogged with dust, and the dust can be directed downstream. It can flow easily and smoothly.

また、本実施形態では、吸入口49は、配置される環状管路48の位置が、吸出口51が設けられる一端(端部48B)から他端(端部48A)に進むほど、吸入口49が設けられる内周面の面積に対する開口率が大きくなるよう形成される。つまり、環状管路48の上流から下流に進むほど吸入口49の開口率が小さくなる。 Further, in the present embodiment, the position of the annular conduit 48 disposed in the suction port 49 increases as the suction port 49 advances from one end (end portion 48B) at which the suction port 51 is provided to the other end (end portion 48A). is formed so that the aperture ratio with respect to the area of the inner peripheral surface provided with is large. That is, the opening ratio of the suction port 49 becomes smaller as it progresses from the upstream to the downstream of the annular conduit 48 .

この構成により、吸入口49の風量が小さくなる環状管路48の始点側では、吸入口49の開口率を大きくすることによって、空気が吸入口49を通過する際の抵抗を小さくして、粉塵を吸い込みやすくできる。一方、吸入口49の風量が大きくなる環状管路48の終点側では、吸入口49の開口率を小さくすることによって、空気が吸入口49を通過する際の抵抗を大きくして、粉塵を吸い込みにくくできる。この結果、上記の断面積を変化させる構成と同様に、環状管路48の流れ方向の全体で、吸入口49からの粉塵の吸い込み量を均一化できる。 With this configuration, on the starting point side of the annular duct 48 where the air volume of the suction port 49 is small, the opening ratio of the suction port 49 is increased to reduce the resistance when the air passes through the suction port 49, thereby reducing the dust. can be easily absorbed. On the other hand, on the end point side of the annular duct 48 where the air volume of the suction port 49 increases, the opening ratio of the suction port 49 is decreased to increase the resistance when the air passes through the suction port 49, thereby sucking dust. It can be done easily. As a result, the amount of dust sucked from the suction port 49 can be made uniform over the entire flow direction of the annular conduit 48, in the same manner as in the configuration that varies the cross-sectional area.

また、環状管路48の上流から下流に進むほど粉塵が各吸入口49から積算されて、管路内を流れる粉塵の量が増加する傾向がある。これに対して本実施形態のように下流側になるほど吸入口49の開口率を小さくすることで、管路48の下流側で新たに積算される粉塵の量を抑制できるので、粉塵が管路に詰まるような事態をさらに防止でき、粉塵を下流側によりスムーズに流れやすくできる。 In addition, as the circular pipeline 48 progresses from the upstream to the downstream, the dust accumulates from each suction port 49, and the amount of dust flowing through the pipeline tends to increase. On the other hand, by decreasing the opening ratio of the suction port 49 toward the downstream side as in the present embodiment, the amount of dust newly accumulated on the downstream side of the pipeline 48 can be suppressed. Clogging can be further prevented, and dust can flow more smoothly downstream.

また、筒状部47の底板56のうちじょうご部46より内側に露出する部分(図5に径方向の幅Dで示す部分)に、じょうご部46の内側と環状管路48との間を連通して、粉粒体24投入に伴い発生する粉塵を環状管路48に吸入する第2吸入口54が、筒状部47の周方向全体に亘って設けられる。 A portion of the bottom plate 56 of the cylindrical portion 47 that is exposed to the inside of the funnel portion 46 (the portion indicated by the radial width D in FIG. 5) communicates between the inside of the funnel portion 46 and the annular conduit 48 . A second suction port 54 is provided along the entire circumferential direction of the cylindrical portion 47 to suck dust generated by the injection of the granular material 24 into the annular conduit 48 .

この構成により、筒状部47の内周面に加えて、底板56からも粉塵を収集できるので、粉粒体24投入時に発生する粉塵をさらに効率よく収集でき、粉粒体24投入時の粉塵発生をより一層効率よく、かつ効果高く抑制できる。 With this configuration, dust can be collected not only from the inner peripheral surface of the cylindrical portion 47 but also from the bottom plate 56, so that the dust generated when the granular material 24 is introduced can be collected more efficiently. The occurrence can be suppressed more efficiently and effectively.

集塵用器具4は、筒状部47と環状管路48とを含む上部部材41と、じょうご部46を含む下部部材42と、を備え、じょうご部46と筒状部47とが重なる位置で、じょうご部46の上端で上部部材41の底板56を支持することで、上部部材41と下部部材42とが一体的に組まれる。 The dust collecting device 4 includes an upper member 41 including a tubular portion 47 and an annular conduit 48, and a lower member 42 including a funnel portion 46. At a position where the funnel portion 46 and the tubular portion 47 overlap, , the bottom plate 56 of the upper member 41 is supported by the upper end of the funnel portion 46, so that the upper member 41 and the lower member 42 are assembled integrally.

この構成により、じょうご部46と筒状部47との接続部など粉塵が堆積しやすい場所を分解でき、堆積した粉塵の除去など集塵用器具4のメンテナンスを容易に行うことができる。 With this configuration, it is possible to dismantle a place where dust tends to accumulate, such as the joint between the funnel portion 46 and the cylindrical portion 47, and facilitate maintenance of the dust collecting device 4, such as removal of accumulated dust.

なお、本実施形態の集塵用器具4は、一つの製造ライン(製造装置)において、異なる種類の材料(粉粒体)を用いた固形製剤を製造するシステム、すなわち、ある(第1の)材料を使用した固形製剤製品を製造し、その後同じ製造ライン(製造装置)において別の(第2の)材料を使用した固形製剤製品を製造するシステムにも適用できる。このような場合においても、排気フードのフード内周面に付着した粉塵の塊が脱離・落下し製品へ混入するようなことがないので、異なる製品の材料(粉粒体)が混入することがない。 In addition, the dust collecting device 4 of the present embodiment is a system for producing solid preparations using different types of materials (granules) in one production line (manufacturing apparatus), that is, a (first) It can also be applied to a system that manufactures a solid formulation product using a material and then manufactures a solid formulation product using another (second) material on the same production line (manufacturing apparatus). Even in such a case, the clumps of dust adhering to the inner peripheral surface of the exhaust hood will not come off or fall and mix into the product. There is no

<実施形態の効果を示す実施例および用途例>
本実施形態に基づく集塵用器具、集塵装置、充填装置を集塵システムとして利用し、対象となる粉粒体として、漢方薬固形製品の原料である0.5μm微粒子と5.0μm微粒子を使用した際の粉塵抑制の効果を示すための実施例を説明する。
<Examples and application examples showing the effect of the embodiment>
The dust collector, dust collector, and filling device based on this embodiment are used as a dust collection system, and 0.5 μm fine particles and 5.0 μm fine particles, which are the raw materials of solid products of Chinese herbal medicine, are used as the target powders and granules. An example will be described to demonstrate the effect of dust suppression when

実施例の各種条件の詳細は下記のとおりである。 The details of various conditions in the examples are as follows.

(実施方法)漢方薬固形製品の充填装置周辺における集塵効果測定
(測定条件)空調システム及び投入ホッパの局所排気装置が通常運転状態である中での清浄度回復確認
(検査対象)固形剤充填設備系統クリーンルーム
(検査目的)作業後設定された基準値内に回復することを確認する
(測定機器)パーティクルカウンター(日本カノマックス社製:校正済み)
(Implementation method) Measurement of the dust collection effect around the filling equipment for herbal medicine solid products (Measurement conditions) Confirmation of cleanness recovery while the air-conditioning system and local exhaust equipment of the injection hopper are in normal operation (Inspection object) Solid drug filling equipment System clean room (Inspection purpose) Confirm that the work is recovered within the set standard value (Measuring equipment) Particle counter (manufactured by Kanomax Japan Co., Ltd.: calibrated)

(判定基準)指定した時間間隔で測定し、測定値がPIC/S GMPガイドラインに規定された下記の表1に記載の清浄度クラスGrade Bを満足するまでに回復する時間を測定する。なお、表1に例示する清浄度クラスとは、ISO14644-1による無菌医薬品の製造における清浄度クラスである。Grade Bとは、無菌の調整や充填の工程に関して、高リスクの作業を行う清浄区域であり、Grade Aのバックグラウンドの環境レベルである。 (Judgment Criteria) Measure at specified time intervals, and measure the recovery time until the measured value satisfies the cleanliness class Grade B listed in Table 1 below specified in the PIC/S GMP guidelines. The cleanliness class exemplified in Table 1 is the cleanliness class in manufacturing sterile pharmaceuticals according to ISO14644-1. Grade B is a clean area with high risk operations and a Grade A background environmental level for aseptic preparation and filling processes.

Figure 0007307920000001
Figure 0007307920000001

(測定方法)充填装置の投入ホッパへ漢方薬固形製品20kgを投入し、その直後(t=0)をワースト条件として、2分おきに室内大気中の微粒子をパーティクルカウンターで測定する。測定結果が2回連続で上記の表1に示す清浄度基準値以下に達した段階で回復したとみなし測定を終了する。 (Measurement method) 20 kg of herbal medicine solid product is put into the feeding hopper of the filling device, and immediately after that (t=0) is set as the worst condition, and the fine particles in the indoor air are measured with a particle counter every 2 minutes. When the measurement result reaches below the cleanliness standard value shown in Table 1 above two times in a row, it is considered to have recovered and the measurement is terminated.

(測定結果)
上記実施例の測定結果を下記の表2に示す。なお、各測定時間に得られた粒子データは、実際の測定風量2.83L/minを1.0m/minに換算している。
(Measurement result)
The measurement results of the above examples are shown in Table 2 below. In the particle data obtained at each measurement time, the actual measured air volume of 2.83 L/min was converted to 1.0 m 3 /min.

Figure 0007307920000002
Figure 0007307920000002

表2に示すように、本清浄度回復試験では、上記判定基準のGrade Bの基準値を速やかに充たす集塵効果が得られた。本結果より、本実施形態に基づく集塵装置等の利用により、対象となる粉粒体の投入時に発生する粉塵を効率よく、効果高く抑制できることが判明した。 As shown in Table 2, in this cleanliness recovery test, a dust collecting effect that quickly satisfied the criteria value of Grade B of the above criteria was obtained. From this result, it was found that the use of the dust collector or the like based on this embodiment can efficiently and effectively suppress the dust generated when the target powder or granular material is charged.

抑制対象となる粉塵発生物質としては、例えば、天然物、鉱物、化学品、食品、医薬品、漢方薬、農薬及びそれらの原料、中間体、最終製品などの粉粒体が挙げられるが、これらの具体例に限定されるものではない。 Dust-generating substances to be suppressed include, for example, natural products, minerals, chemicals, foods, pharmaceuticals, herbal medicines, agricultural chemicals, and powders such as raw materials, intermediates, and final products thereof. Examples are not limiting.

また、本実施形態に基づき対象となる粉粒体の粉塵発生を抑制することにより、集塵システムの系外にある物質へのコンタミネーションを抑制するとともに、大気・水質・土壌への拡散による環境汚染を抑制し、あるいは粉塵吸入抑制、粉塵爆発抑制など作業者安全対策にも役立つ。 In addition, by suppressing the generation of dust from the target powder and granular material based on this embodiment, contamination with substances outside the system of the dust collection system is suppressed, and the environment due to diffusion into the air, water, and soil It is also useful for worker safety measures such as suppressing contamination, suppressing dust inhalation, and suppressing dust explosion.

さらに、本実施形態に基づく集塵システムおよび固形製剤製造装置を利用することにより、製造過程で生成される粉粒体中の微細な粉塵の除去が可能となり、最終固形製剤製品の品質を向上させることができる。 Furthermore, by using the dust collection system and the solid preparation manufacturing apparatus based on this embodiment, it becomes possible to remove fine dust in the granules generated in the manufacturing process, and the quality of the final solid preparation product is improved. be able to.

以上、具体例を参照しつつ本実施形態について説明した。しかし、本開示はこれらの具体例に限定されるものではない。これら具体例に、当業者が適宜設計変更を加えたものも、本開示の特徴を備えている限り、本開示の範囲に包含される。前述した各具体例が備える各要素およびその配置、条件、形状などは、例示したものに限定されるわけではなく適宜変更することができる。前述した各具体例が備える各要素は、技術的な矛盾が生じない限り、適宜組み合わせを変えることができる。 The present embodiment has been described above with reference to specific examples. However, the present disclosure is not limited to these specific examples. Design modifications to these specific examples by those skilled in the art are also included in the scope of the present disclosure as long as they have the features of the present disclosure. Each element included in each specific example described above and its arrangement, conditions, shape, etc. are not limited to those illustrated and can be changed as appropriate. As long as there is no technical contradiction, the combination of the elements included in the specific examples described above can be changed as appropriate.

上記実施形態では、集塵用器具4の環状管路48に粉塵を吸入する要素として、筒状部47の内周面に設けられる吸入口49と、環状管路48の底板56に設けられる第2吸入口54の2種類の吸入口を備える構成を例示したが、少なくとも吸入口49を備える構成であればよい。 In the above-described embodiment, as elements for sucking dust into the annular conduit 48 of the dust collecting device 4 , the suction port 49 provided on the inner peripheral surface of the cylindrical portion 47 and the second nozzle provided on the bottom plate 56 of the annular conduit 48 are provided. Although the configuration provided with two types of suction ports, ie, the two suction ports 54, is illustrated, a configuration including at least the suction port 49 may be used.

上記実施形態では、集塵用器具4が上部部材41と下部部材42とで分解可能な構成を例示したが、一体的に形成される構成でもよい。 In the above-described embodiment, the configuration in which the dust collecting device 4 can be disassembled into the upper member 41 and the lower member 42 was exemplified, but a configuration in which it is integrally formed is also possible.

集塵用器具4が充填装置2の投入口21に一体的に設けられる場合には、集塵用器具4の上部部材41に相当する部分のみでもよい。 When the dust collecting device 4 is provided integrally with the inlet 21 of the filling device 2, only the portion corresponding to the upper member 41 of the dust collecting device 4 may be used.

集塵用器具4の吸出口51の配置は、図6に点線で示した吸出口51aのように、その軸線が筒状部47の中心を通る位置に設けられてもよい。 The suction port 51 of the dust collecting device 4 may be arranged such that its axis passes through the center of the tubular portion 47, like the suction port 51a indicated by the dotted line in FIG.

上記実施形態では、筒状部47の内周面に設けられる吸入口49の開口率を環状管路48の位置に応じて変更する構成を例示したが、内周面の全域に亘って吸入口49の開口率を均一にしてもよい。 In the above-described embodiment, the opening ratio of the suction port 49 provided on the inner peripheral surface of the tubular portion 47 is changed according to the position of the annular conduit 48. 49 may have a uniform aperture ratio.

1 集塵システム
2 充填装置(固形製剤製造装置)
24 粉粒体
3 集塵装置
4 集塵用器具
41 上部部材(第1部材)
42 下部部材(第2部材)
46 じょうご部
47 筒状部
48 環状管路
49 吸入口
50 筐体
51 吸出口
54 第2吸入口
56 底板(接続部)
5 空気吸出し装置
6 空気供給装置
1 dust collection system 2 filling device (solid preparation manufacturing device)
24 Granular material 3 Dust collector 4 Dust collector 41 Upper member (first member)
42 Lower member (second member)
46 funnel portion 47 cylindrical portion 48 annular conduit 49 suction port 50 housing 51 suction port 54 second suction port 56 bottom plate (connecting portion)
5 air suction device 6 air supply device

Claims (11)

粉粒体が投入される装置の投入口に設置される集塵用器具であって、
前記粉粒体が通過する筒状部と、
前記筒状部の外周側に設けられる環状管路と、
前記筒状部の内周面の周方向全体に亘って設けられ、前記筒状部の内側と前記環状管路との間を連通して、粉粒体投入に伴い発生する粉塵を前記環状管路に吸入する吸入口と、
前記環状管路の一端に設けられ外部と連通し、前記環状管路に吸引した前記粉塵を外部に吸い出すための吸出口と、
を備え
前記環状管路は、前記吸出口が設けられる前記一端から他端に進むほど断面積が小さくなるよう形成される、
集塵用器具。
A dust collection device installed at an inlet of a device into which powder or granular material is introduced,
a tubular portion through which the granular material passes;
an annular pipeline provided on the outer peripheral side of the cylindrical portion;
It is provided over the entire circumferential direction of the inner peripheral surface of the cylindrical portion, and communicates between the inner side of the cylindrical portion and the annular conduit to remove dust generated along with the introduction of powder or granular material into the annular conduit. an inlet for inhaling into the passage;
a suction port provided at one end of the annular conduit and communicating with the outside for sucking out the dust sucked into the annular conduit ;
with
The annular conduit is formed so that the cross-sectional area decreases as it progresses from the one end where the suction port is provided to the other end.
Dust collector.
前記筒状部及び前記環状管路が円環形状であり、
前記吸出口は、前記吸出口の軸線方向が前記筒状部の前記円環形状の接線方向と平行であり、かつ、前記筒状部の中心からずれる位置に設けられる、
請求項1に記載の集塵用器具。
The tubular portion and the annular pipeline are annular,
The suction port is provided at a position where the axial direction of the suction port is parallel to the tangential direction of the annular shape of the cylindrical portion and is deviated from the center of the cylindrical portion.
The dust collecting device according to claim 1.
前記筒状部の外周側に設けられる筐体を備え、
前記環状管路は、前記筒状部を形成する内壁と、前記筐体の外壁とで形成され、
前記粉粒体の投入方向から視たときに、前記筐体の中央位置に対して前記筒状部の軸心位置をずらすことにより、前記吸出口が設けられる前記一端から前記他端に進むほど前記内壁と前記外壁との距離が小さくなるよう形成される、
請求項に記載の集塵用器具。
A housing provided on the outer peripheral side of the tubular portion,
The annular conduit is formed by an inner wall forming the cylindrical portion and an outer wall of the housing,
By shifting the axial center position of the cylindrical portion with respect to the center position of the housing when viewed from the charging direction of the powder or granular material, it is possible to move from the one end where the suction port is provided to the other end. formed so that the distance between the inner wall and the outer wall is small,
The dust collecting device according to claim 2 .
前記吸入口は、配置される前記環状管路の位置が、前記吸出口が設けられる前記一端から前記他端に進むほど、前記吸入口が設けられる前記内周面の面積に対する開口率が大きくなるよう形成される、
請求項1~のいずれか1項に記載の集塵用器具。
The opening ratio of the suction port with respect to the area of the inner peripheral surface provided with the suction port increases as the position of the annular conduit arranged advances from the one end where the suction port is provided to the other end. formed like,
A dust collecting device according to any one of claims 1 to 3 .
粉粒体が投入される装置の投入口に設置される集塵用器具であって、
前記粉粒体が通過する筒状部と、
前記筒状部の外周側に設けられる環状管路と、
前記筒状部の内周面の周方向全体に亘って設けられ、前記筒状部の内側と前記環状管路との間を連通して、粉粒体投入に伴い発生する粉塵を前記環状管路に吸入する吸入口と、
前記環状管路の一端に設けられ外部と連通する吸出口と、
を備え、
前記吸入口は、配置される前記環状管路の位置が、前記吸出口が設けられる前記一端から他端に進むほど、前記吸入口が設けられる前記内周面の面積に対する開口率が大きくなるよう形成され、
前記粉粒体の投入方向の前記筒状部より下流側に前記筒状部と連結して設けられ、前記筒状部を通過した前記粉粒体が投入されるじょうご部を備え、
前記筒状部の前記内周面は、前記じょうご部の前記筒状部側の端部より中心側に突出しており、前記筒状部の前記じょうご部側の端部と、前記じょうご部の前記筒状部側の前記端部とを接続する接続部が設けられ、
前記接続部には、前記じょうご部の内側と前記環状管路との間を連通して、粉粒体投入に伴い発生する粉塵を前記環状管路に吸入する第2吸入口が前記筒状部の周方向全体に亘って設けられる
塵用器具。
A dust collection device installed at an inlet of a device into which powder or granular material is introduced,
a tubular portion through which the granular material passes;
an annular pipeline provided on the outer peripheral side of the cylindrical portion;
It is provided over the entire circumferential direction of the inner peripheral surface of the cylindrical portion, and communicates between the inner side of the cylindrical portion and the annular conduit to remove dust generated along with the introduction of powder or granular material into the annular conduit. an inlet for inhaling into the passage;
a suction port provided at one end of the annular conduit and communicating with the outside;
with
The suction port is arranged such that the opening ratio with respect to the area of the inner peripheral surface where the suction port is provided increases as the position of the annular conduit arranged advances from the one end where the suction port is provided to the other end. formed,
a funnel portion provided downstream of the cylindrical portion in the charging direction of the powder or granular material and connected to the cylindrical portion, into which the powder or granular material that has passed through the cylindrical portion is charged;
The inner peripheral surface of the cylindrical portion protrudes toward the center from the end portion of the funnel portion on the cylindrical portion side. A connecting portion is provided to connect the end portion on the cylindrical portion side,
The connecting portion includes a second suction port that communicates between the inside of the funnel portion and the annular pipeline and sucks dust generated by charging the granular material into the annular pipeline. provided over the entire circumferential direction of
Dust collector.
前記筒状部と前記環状管路とを含む第1部材と、
前記じょうご部を含む第2部材と、を備え、
前記じょうご部と前記筒状部とが重なる位置で、前記じょうご部の前記端部で前記第1部材の底板を支持することで前記第1部材と前記第2部材とが一体的に組まれる、
請求項に記載の集塵用器具。
a first member including the tubular portion and the annular conduit;
a second member including the funnel,
The first member and the second member are integrally assembled by supporting the bottom plate of the first member at the end portion of the funnel portion at a position where the funnel portion and the cylindrical portion overlap,
The dust collecting device according to claim 5 .
請求項1~のいずれか1項に記載の集塵用器具と、
前記集塵用器具の前記吸出口に接続され、前記環状管路内の空気を吸い出す空気吸出し装置と、
を有する集塵装置。
A dust collecting device according to any one of claims 1 to 6 ,
an air suction device connected to the suction port of the dust collecting device and sucking air in the annular conduit;
A dust collector with
前記集塵用器具より投入側に設けられ、フィルタ装置により洗浄された洗浄空気を前記集塵用器具の方向へ送出する空気供給装置を備える、
請求項に記載の集塵装置。
An air supply device is provided on the inlet side of the dust collecting device and feeds cleaning air washed by the filter device toward the dust collecting device,
The dust collector according to claim 7 .
投入口に投入される粉粒体を袋体に充填して固形製剤を出力する固形製剤製造装置であって、
請求項1~のいずれか1項に記載の集塵用器具が前記投入口に設置される
固形製剤製造装置。
A solid preparation manufacturing apparatus for outputting a solid preparation by filling a bag with powder or granules fed into an inlet,
A solid preparation manufacturing apparatus, wherein the dust collection device according to any one of claims 1 to 6 is installed at the inlet.
投入口に投入される粉粒体を袋体に充填して出力する充填装置と、
前記投入口に前記集塵用器具が設置された請求項7または8に記載の集塵装置と、
を備える集塵システム。
a filling device that fills a bag with powder or granular material that is fed into the inlet and outputs the bag;
9. The dust collector according to claim 7 or 8 , wherein the dust collecting device is installed at the input port;
dust collection system.
粉粒体が通過する筒状部と、前記筒状部の外周側に設けられる環状管路と、前記筒状部の内周面の周方向全体に亘って設けられ、前記筒状部の内側と前記環状管路との間を連通して、粉粒体投入に伴い発生する粉塵を前記環状管路に吸入する吸入口と、前記環状管路の一端に設けられ外部と連通し、前記環状管路に吸引した前記粉塵を外部に吸い出すための吸出口と、を備え、前記環状管路は、前記吸出口が設けられる前記一端から他端に進むほど断面積が小さくなるよう形成される、集塵用器具を、前記粉粒体が投入される装置の投入口に設置するステップと、
前記集塵用器具の前記吸出口に空気吸出し装置を接続して、前記環状管路内の空気を吸い出すステップと、
前記投入口に投入される前記粉粒体を袋体に充填して固形製剤を出力するステップと、を含む固形製剤製造方法。
A cylindrical portion through which the powder or granular material passes; an annular pipeline provided on the outer peripheral side of the cylindrical portion; and the annular pipeline, a suction port for sucking dust generated by the introduction of powder or granular material into the annular pipeline, and a suction port provided at one end of the annular pipeline and communicating with the outside, the annular and a suction port for sucking the dust sucked into the pipe to the outside , and the annular pipe is formed so that the cross-sectional area becomes smaller as it progresses from the one end where the suction port is provided to the other end. A step of installing a dust collecting device at an inlet of a device into which the granular material is introduced;
a step of connecting an air suction device to the suction port of the dust collecting device to suck out the air in the annular conduit;
a step of filling a bag with the powder or granular material introduced into the inlet and outputting a solid preparation.
JP2019177541A 2018-09-28 2019-09-27 Dust collector, dust collector, solid preparation manufacturing device, dust collection system, and solid preparation manufacturing method Active JP7307920B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2018185397 2018-09-28
JP2018185397 2018-09-28

Publications (2)

Publication Number Publication Date
JP2020055642A JP2020055642A (en) 2020-04-09
JP7307920B2 true JP7307920B2 (en) 2023-07-13

Family

ID=70106665

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2019177541A Active JP7307920B2 (en) 2018-09-28 2019-09-27 Dust collector, dust collector, solid preparation manufacturing device, dust collection system, and solid preparation manufacturing method

Country Status (1)

Country Link
JP (1) JP7307920B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114229250A (en) * 2021-11-18 2022-03-25 江苏千里机械有限公司 Environment-friendly lime feed bin
JP2024033717A (en) * 2022-08-31 2024-03-13 ケンブリッジフィルターコーポレーション株式会社 dust collection hood

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003206036A (en) 2002-01-15 2003-07-22 Mitsubishi Heavy Ind Ltd Unloader and dust collecting method for bulk (bulk cargo) in unloader
JP2004123116A (en) 2002-09-30 2004-04-22 Kyowa Exeo Corp Granule input structure
JP2005263468A (en) 2004-03-22 2005-09-29 Fuji Tekku Kk Hopper device provided with dust preventing function
JP2007039111A (en) 2005-08-04 2007-02-15 Yuyama Manufacturing Co Ltd Medicine dose packaging apparatus
JP2011245442A (en) 2010-05-28 2011-12-08 Toyota Boshoku Corp Filtration apparatus

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4727057Y1 (en) * 1970-05-06 1972-08-18
JPS57103118U (en) * 1980-12-16 1982-06-25
JP3117155B2 (en) * 1991-10-16 2000-12-11 株式会社ダイヘン Cyclone type dust collector
DE10223220B3 (en) * 2002-05-24 2004-02-26 Hecht Anlagenbau Gmbh Device for filling a container equipped with an inner bag with a bulk material

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003206036A (en) 2002-01-15 2003-07-22 Mitsubishi Heavy Ind Ltd Unloader and dust collecting method for bulk (bulk cargo) in unloader
JP2004123116A (en) 2002-09-30 2004-04-22 Kyowa Exeo Corp Granule input structure
JP2005263468A (en) 2004-03-22 2005-09-29 Fuji Tekku Kk Hopper device provided with dust preventing function
JP2007039111A (en) 2005-08-04 2007-02-15 Yuyama Manufacturing Co Ltd Medicine dose packaging apparatus
JP2011245442A (en) 2010-05-28 2011-12-08 Toyota Boshoku Corp Filtration apparatus

Also Published As

Publication number Publication date
JP2020055642A (en) 2020-04-09

Similar Documents

Publication Publication Date Title
KR101604146B1 (en) Spinning air sieving method and device
JP7307920B2 (en) Dust collector, dust collector, solid preparation manufacturing device, dust collection system, and solid preparation manufacturing method
CN101366616A (en) Cyclone separation device
CN101274309A (en) Cyclone separation device
CN104755185B (en) The segregation apparatuss of the material of absorbent commodity
KR101541921B1 (en) Powder removal device and steric separation system
CN104755184A (en) Method for separating and device for separating material pertaining to absorbent article
SE1250197A1 (en) Method for calibrating a device for dispensing granular or powdery material and such device
CN110121625A (en) The powder drying system of improvement inlet device with filter unit and the method that the filter unit of this system is operated
EP2078488A2 (en) Device to remove dust from air full of dust, especially for use in a vacuum cleaner
JP6283021B2 (en) Powder classification device and powder classification system
CN207357600U (en) A kind of cereal selection by winnowing agricultural machinery
EP2537450A1 (en) Dust trap
CN111359315B (en) Dust removal equipment
CN213700791U (en) Material sorting and suction device
CN211521029U (en) Glass raw material dust removal system
CN116941420A (en) Tea leaf picking device
KR101536694B1 (en) Separator for sorting particulate material
US20110030558A1 (en) Dust collector, filtration arrangment, and methods
CN211755511U (en) a fiber separator
CN113996534B (en) Environment-friendly hopper with grain separation function
JP4932858B2 (en) Particulate matter removal device
CN217528206U (en) Screening machine is used in fertilizer processing
CN223658460U (en) A dust collector cover for a feed inlet
CN208150507U (en) Powder blanking exhaust apparatus and dust collecting

Legal Events

Date Code Title Description
RD01 Notification of change of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7426

Effective date: 20191023

AA64 Notification of invalidation of claim of internal priority (with term)

Free format text: JAPANESE INTERMEDIATE CODE: A241764

Effective date: 20191029

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20191101

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20191023

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20191101

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20191213

A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20220221

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20230124

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20230131

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20230329

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20230530

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20230623

R150 Certificate of patent or registration of utility model

Ref document number: 7307920

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150