JP2009227431A - Transfer device for granular solid - Google Patents

Transfer device for granular solid Download PDF

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JP2009227431A
JP2009227431A JP2008077093A JP2008077093A JP2009227431A JP 2009227431 A JP2009227431 A JP 2009227431A JP 2008077093 A JP2008077093 A JP 2008077093A JP 2008077093 A JP2008077093 A JP 2008077093A JP 2009227431 A JP2009227431 A JP 2009227431A
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casing
suspension
spiral blade
granular solid
granular
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JP5376820B2 (en
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Yoshifumi Nagasawa
吉史 長沢
Akihiro Yamamoto
明宏 山本
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Nikko Co Ltd
Nikko KK
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Nikko Co Ltd
Nikko KK
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a transfer device for a granular solid which can effectively separate a suspension without deteriorating transfer efficiency when the granular solid is transferred from the suspension containing the granular solid, and is convenient even in a maintenance aspect. <P>SOLUTION: An approximately cylindrical casing 4 is inclined and arranged so that a discharge port 3 side becomes high, a storage hopper 5 for storing the suspension is connected to a throwing port 2 of the casing 4, and a ribbon-like helical impeller 7 having a hollow part 6 formed along an axis is internally installed in the casing 4. Furthermore, an upper end of the helical impeller 7 is only fixed to a drive shaft 9, whereby a lower end is made as a free end without fixing, and a canti-lever structure is formed. A plurality of reinforcement members 12 are fixed to an inner peripheral edge facing an axis hollow part 6 of the helical impeller 7 to apply reinforcement. Furthermore, when the granular solid is pulled up to the discharge port 3 side of an upper end of the casing 4 to be transferred, the suspension associated with the granular solid is made to flow down from the axis hollow part 6 of the helical impeller 7 to effectively be separated. <P>COPYRIGHT: (C)2010,JPO&INPIT

Description

本発明は、粒状固形物を含む懸濁液から粒状固形物を分離して移送する粒状固形物の移送装置に関する。   The present invention relates to a granular solid material transfer device for separating and transferring a granular solid material from a suspension containing the granular solid material.

従来、各種スラリーやスラッジ水、泥水等、様々な粒状固形物を含んだ懸濁液から粒状固形物を分離して移送する装置として、例えば、特許文献1〜3に示すように、排出口側が高くなるように傾斜配置したスクリューコンベヤの投入口に懸濁液貯留用の貯留ホッパを連結したものがある。上記移送装置においては、懸濁液を貯留した貯留ホッパ底部に沈殿する各種粒状固形物を、ホッパ底部に連結したスクリューコンベヤにて斜め上方向の排出口側へ押し上げて移送するようにしており、その移送の際には、粒状固形物に随伴する多量の懸濁液をスクリュー羽根外周縁とコンベヤのケーシング内壁とのクリアランスより流下させて液切りし、分離させるように図っている。
特開平6−11125号公報 特開2000−317694号公報 実公平3−30332号公報
Conventionally, as an apparatus for separating and transferring granular solids from a suspension containing various granular solids such as various slurries, sludge water, and muddy water, for example, as shown in Patent Documents 1 to 3, the outlet side is There is one in which a storage hopper for storing suspension is connected to an inlet of a screw conveyor that is inclined so as to be higher. In the above transfer device, various granular solids that settle on the bottom of the storage hopper storing the suspension are pushed up and transferred to the discharge port side obliquely upward by a screw conveyor connected to the bottom of the hopper, At the time of the transfer, a large amount of suspension accompanying the particulate solid is made to flow down from the clearance between the outer peripheral edge of the screw blade and the inner wall of the casing of the conveyor to be drained and separated.
JP-A-6-11125 JP 2000-317694 A Japanese Utility Model Publication No. 3-30332

ところで、粒状固形物や懸濁液の用途等によってはそれぞれを極力分離させることが要求される場合があり、それを上記従来装置で対応しようとすれば、例えば、コンベヤの移送速度を落として懸濁液が流下するための時間を多く稼ぐようにしたり、或いは羽根外周縁とケーシング内壁とのクリアランスを広くして懸濁液が流下しやすいように調整すること等が考えられるが、このような調整は粒状固形物の移送効率の低下を来すため必ずしも好ましいものとは言えない。また、傾斜配置したスクリューコンベヤの下位側軸受部は懸濁液中に浸漬し、絶えず懸濁液に曝される構成であるため、懸濁液の漏洩防止に高いシール性が求められる上、軸受部内への粒状固形物の侵入によってベアリング等の損耗が極端に早まってしまうといったメンテナンス上の問題も有している。なお、特許文献3の移送装置においては、下位側軸受部のハウジング内に加圧液を供給することによって粒状固形物の侵入を防ぐように図っているものの、構造が複雑化してコストアップが懸念される上、軸受部が懸濁液に曝されている点では依然として変わりがないため、粒状固形物の侵入を完全に阻止するのは難しいものと考えられる。   By the way, depending on the use of granular solids and suspension, etc., it may be required to separate them as much as possible. It may be possible to gain a lot of time for the turbid liquid to flow down, or to adjust the clearance between the blade outer peripheral edge and the casing inner wall so that the suspension can easily flow down. Adjustment is not necessarily preferable because it causes a decrease in the transfer efficiency of the granular solid. In addition, since the lower bearing portion of the screw conveyor that is inclined is immersed in the suspension and constantly exposed to the suspension, high sealability is required to prevent leakage of the suspension. There is also a maintenance problem that the wear of the bearing or the like is extremely accelerated due to the intrusion of the granular solid into the part. In addition, although the transfer device of Patent Document 3 is designed to prevent intrusion of granular solids by supplying pressurized liquid into the housing of the lower bearing portion, there is a concern that the structure becomes complicated and the cost increases. In addition, it is considered that it is difficult to completely prevent the intrusion of the particulate solid because the bearing is still unchanged in that it is exposed to the suspension.

本発明は上記の点に鑑み、粒状固形物を含む懸濁液から粒状固形物を移送する際、移送効率を低下させることなく懸濁液を効果的に分離できると共に、メンテナンス面においても好適な粒状固形物の移送装置を提供することを課題とする。   In view of the above points, the present invention can effectively separate a suspension without lowering the transfer efficiency when transferring a granular solid from a suspension containing the granular solid, and is also suitable in terms of maintenance. It is an object of the present invention to provide a granular solid material transfer device.

上記課題を解決するために、本発明に係る粒状固形物の移送装置では、粒状固形物を含む懸濁液から粒状固形物を分離して移送する粒状固形物の移送装置であって、一端部に投入口を他端部に排出口を備えた略円筒形状のケーシングを排出口側が高くなるように傾斜配置し、該ケーシングの投入口には懸濁液貯留用の貯留ホッパを連結すると共に、ケーシング内部には軸心に沿って中空部が形成されるリボン状螺旋羽根を内装し、該螺旋羽根の上端部はケーシング上端側より貫通させて回転自在に軸支した駆動軸に固着する一方、螺旋羽根の下端部は固着せずに自由端とし、かつ螺旋羽根の軸心中空部に面する内周縁には複数の補強部材を軸心と平行に螺旋羽根の略全長に亘って固着し、前記螺旋羽根の回転によって懸濁液に含まれる粒状固形物をケーシング上端の排出口側へ引き上げて移送するときには、粒状固形物に随伴する懸濁液を螺旋羽根の軸心中空部よりケーシング下端側へ流下させて分離するように構成したことを特徴としている。   In order to solve the above problems, the granular solids transfer device according to the present invention is a granular solids transfer device that separates and transfers granular solids from a suspension containing the granular solids, and has one end. A substantially cylindrical casing provided with a discharge port at the other end is inclined so that the discharge port side is higher, and a storage hopper for storing suspension is connected to the input port of the casing, Inside the casing is a ribbon-like spiral blade having a hollow portion formed along the shaft center, and the upper end of the spiral blade is penetrated from the upper end side of the casing and fixed to a drive shaft rotatably supported. The lower end portion of the spiral blade is not fixed, and is a free end, and a plurality of reinforcing members are fixed to the inner peripheral edge facing the hollow portion of the axial center of the spiral blade over substantially the entire length of the spiral blade in parallel with the axial center, The granular solid contained in the suspension by the rotation of the spiral blade When the product is lifted and transferred to the discharge port side at the upper end of the casing, the suspension accompanying the particulate solid is flowed down to the lower end side of the casing from the axial hollow portion of the spiral blade and separated. Yes.

本発明に係る粒状固形物の移送装置によれば、一端部に投入口を他端部に排出口を備えた略円筒形状のケーシングを排出口側が高くなるように傾斜配置し、該ケーシングの投入口には懸濁液貯留用の貯留ホッパを連結すると共に、ケーシング内部には軸心に沿って中空部が形成されるリボン状螺旋羽根を内装し、該螺旋羽根の上端部はケーシング上端側より貫通させて回転自在に軸支した駆動軸に固着する一方、螺旋羽根の下端部は固着せずに自由端とし、かつ螺旋羽根の軸心中空部に面する内周縁には複数の補強部材を軸心と平行に螺旋羽根の略全長に亘って固着し、前記螺旋羽根の回転によって懸濁液に含まれる粒状固形物をケーシング上端の排出口側へ引き上げて移送するときには、粒状固形物に随伴する懸濁液を螺旋羽根の軸心中空部よりケーシング下端側へ流下させて分離するように構成したので、粒状固形物の移送効率を低下させることなく随伴する懸濁液を効果的に分離できると共に、懸濁液に軸受部が曝されるといったことがなくメンテナンス面において好適である。   According to the granular solids transfer device of the present invention, a substantially cylindrical casing having an inlet at one end and an outlet at the other end is inclined so that the outlet side becomes higher, and the casing is charged. A suspension hopper for storing suspension is connected to the mouth, and a ribbon-like spiral blade having a hollow portion formed along the axial center is provided inside the casing, and the upper end of the spiral blade is from the upper end side of the casing. The lower end of the spiral blade is not fixed, but is a free end, and a plurality of reinforcing members are provided on the inner peripheral edge facing the hollow center of the spiral blade. When the spiral blades are fixed over the entire length in parallel with the axial center, and the solid particles contained in the suspension are lifted and transferred to the discharge port side at the upper end of the casing by the rotation of the spiral blades, they are accompanied by the particulate solids. Axis hollow of the spiral blade that makes the suspension Since it is configured to flow down to the lower end side of the casing for separation, the accompanying suspension can be effectively separated without lowering the transfer efficiency of the granular solid, and the bearing portion is exposed to the suspension. This is preferable in terms of maintenance.

本発明の粒状固形物の移送装置にあっては、一端部に投入口を他端部に排出口を備えた略円筒形状のケーシングを排出口側が高くなるように傾斜配置し、該ケーシングの投入口には懸濁液の貯留ホッパを連結すると共に、ケーシング内部には軸心に沿って中空部が形成されるリボン状螺旋羽根を内装している。また、前記螺旋羽根の上端部はケーシング上端側より貫通させて回転自在に軸支した駆動軸に固着している一方、螺旋羽根の下端部は回転軸等には固着せずに自由端とし、所謂片持ち構造を採用している。また、螺旋羽根の軸心中空部に面する内周縁には複数の補強部材を軸心と平行にかつ螺旋羽根の略全長に亘って固着している。   In the granular solids transfer device of the present invention, a substantially cylindrical casing having an inlet at one end and an outlet at the other end is inclined so that the outlet side becomes higher, and the casing is charged. A suspension storage hopper is connected to the mouth, and a ribbon-like spiral blade having a hollow portion formed along the axial center is provided inside the casing. Further, the upper end portion of the spiral blade is fixed to a drive shaft that is rotatably supported by penetrating from the upper end side of the casing, while the lower end portion of the spiral blade is a free end without being fixed to the rotation shaft, etc. A so-called cantilever structure is employed. Further, a plurality of reinforcing members are fixed to the inner peripheral edge facing the hollow portion of the axial center of the spiral blade in parallel with the axial center and over substantially the entire length of the spiral blade.

そして、上記移送装置を使用して粒状固形物を含んだ懸濁液から粒状固形物を分離して移送するときには、先ず、貯留ホッパに懸濁液を投入して貯留させ、ホッパ底部に沈殿する粒状固形物を下位の円筒状ケーシング内に投入させる。そして、ケーシング内に投入された粒状固形物は、リボン状螺旋羽根の回転駆動によりケーシングに沿って斜め上方向へと順次引き上げられて移送されていくが、その際、粒状固形物に随伴する多量の懸濁液は、螺旋羽根外周縁とケーシング内壁とのクリアランスと、螺旋羽根の軸心に沿って形成された大径の中空部とからケーシング下端側へと比較的素早く流下していくため、例えば、螺旋羽根の移送速度を落としたり、螺旋羽根外周縁とケーシング内壁とのクリアランスを広くするような、わざわざ粒状固形物の移送効率の低下を来すような調整をしなくても、効果的に分離させることができる。   Then, when separating and transferring the granular solid from the suspension containing the granular solid using the transfer device, first, the suspension is put into the storage hopper and stored, and settled at the bottom of the hopper. The granular solid is charged into the lower cylindrical casing. The granular solids put into the casing are sequentially pulled up and transferred along the casing by the rotational drive of the ribbon-shaped spiral blades, and at that time, a large amount accompanying the granular solids. Since the suspension of, the clearance between the outer peripheral edge of the spiral blade and the inner wall of the casing, and the large-diameter hollow portion formed along the axis of the spiral blade, flows down relatively quickly to the lower end of the casing. For example, it is effective without reducing the transfer speed of the spiral blades or widening the clearance between the outer periphery of the spiral blades and the inner wall of the casing. Can be separated.

また、本移送装置では、螺旋羽根の上端部のみを駆動軸に固着し、下端部は自由端とした片持ち構造を採用しており、ケーシング下端側には螺旋羽根を軸支するための軸受部が存在しないため、軸受部からの懸濁液の漏洩や軸受部のベアリングの極端な損耗等といった問題が起こり得ず、メンテナンス面において極めて好適なものとしている。なお、前記リボン状螺旋羽根は、軸心部に羽根支持用の軸体を元々有さない上、羽根上端部のみを固定する片持ち構造を採用しているが、逆に軸体を有さないことによる大幅な軽量化と、軸心中空部に面する螺旋羽根内周縁に固着した複数の補強部材による補強とにより、粒状固形物の移送時のように羽根に大きな負荷が掛かる場合でも湾曲や変形等が生じないように図っている。   In addition, this transfer device employs a cantilever structure in which only the upper end portion of the spiral blade is fixed to the drive shaft and the lower end portion is a free end, and a bearing for supporting the spiral blade on the lower end side of the casing. Since there is no portion, problems such as leakage of suspension from the bearing portion and extreme wear of the bearing portion of the bearing cannot occur, which is extremely suitable in terms of maintenance. The ribbon-shaped spiral blade does not originally have a shaft body for supporting the blade at the shaft center portion, and adopts a cantilever structure that fixes only the upper end portion of the blade, but conversely has a shaft body. Even when a large load is applied to the blade, such as during the transfer of granular solids, the weight is reduced significantly due to the absence and reinforcement by a plurality of reinforcing members fixed to the inner peripheral edge of the spiral blade facing the hollow portion of the shaft center. And so that no deformation or the like occurs.

このように、懸濁液に含まれる粒状固形物を移送する手段として、軸心に沿って大きな中空部が形成されるリボン状の螺旋羽根を採用すると共に、該螺旋羽根の上端部のみを駆動軸に固着して片持ち構造とすることでケーシング下端側の軸受部を不要としたので、粒状固形物の移送効率を低下させることなく軸心中空部から懸濁液を素早く流下させて効果的に分離できると共に、懸濁液に曝されることによる軸受部からの懸濁液の漏洩やベアリングの極端な損耗といった問題が起こり得ず、メンテナンス面において極めて好適である。   As described above, a ribbon-shaped spiral blade having a large hollow portion formed along the axial center is adopted as a means for transferring the granular solid contained in the suspension, and only the upper end portion of the spiral blade is driven. Since the bearing part at the lower end of the casing is not required by fixing the shaft to the cantilever structure, the suspension can be quickly flowed down from the hollow part of the shaft center without reducing the transfer efficiency of granular solids. In addition, there are no problems such as leakage of the suspension from the bearing due to exposure to the suspension and extreme wear of the bearing, which is extremely suitable in terms of maintenance.

以下、本発明の実施例を図面に基づいて説明する。   Embodiments of the present invention will be described below with reference to the drawings.

図中の1は、例えば、各種スラリーやスラッジ水、泥水等、様々な粒状固形物を含んだ懸濁液から粒状固形物を分離して移送する移送装置であって、一端部に投入口2を他端部に排出口3を備えた略円筒形状のケーシング4を、図1に示すように、排出口3側が高くなるように適宜角度にて傾斜配置しており、該ケーシング4の投入口2上位には懸濁液貯留用の貯留ホッパ5を連結していると共に、ケーシング4内部には軸心に沿って比較的大径の中空部6が形成される、粒状固形物移送用のリボン状螺旋羽根7を内装している。   Reference numeral 1 in the figure denotes a transfer device that separates and transfers granular solids from a suspension containing various granular solids such as various slurries, sludge water, and muddy water. As shown in FIG. 1, a substantially cylindrical casing 4 having a discharge port 3 at the other end is inclined at an appropriate angle so that the discharge port 3 side becomes higher. 2 is connected to a storage hopper 5 for storing suspension, and a ribbon for transferring solid solid matter, in which a hollow portion 6 having a relatively large diameter is formed along the axis in the casing 4. A spiral blade 7 is included.

前記ケーシング4の上端部には駆動用モータ8を備え付け、該駆動用モータ8の駆動に応じて駆動チェーン等を介して回転する駆動軸9を、ケーシング4上端外側よりケーシング4内部へと貫通させて回転自在に軸支しており、前記螺旋羽根7の上端部をこの駆動軸9に固着して、駆動軸9の回転に応じて螺旋羽根7を所望速度にて回転させるようにしている一方、螺旋羽根7の下端部は回転軸等には一切固着せずに自由端として、所謂片持ち構造を採用しており、ケーシング4下端側には軸受部が存在しない構成としている。また、ケーシング4下端部には貯留ホッパ5内の残液抜き取り用の抜き取り口10を備えている。   A drive motor 8 is provided at the upper end of the casing 4, and a drive shaft 9 that rotates via a drive chain or the like according to the drive of the drive motor 8 is passed through the casing 4 from the outer side of the upper end of the casing 4. The upper end of the spiral blade 7 is fixed to the drive shaft 9, and the spiral blade 7 is rotated at a desired speed according to the rotation of the drive shaft 9. The lower end portion of the spiral blade 7 is not fixed to the rotating shaft or the like, but has a so-called cantilever structure as a free end, and the bearing 4 does not exist on the lower end side of the casing 4. In addition, the lower end portion of the casing 4 is provided with an extraction port 10 for extracting residual liquid in the storage hopper 5.

なお、螺旋羽根7の外周縁とケーシング4内壁との間には適度な広さのクリアランス11を確保しており、該クリアランス11の存在によって螺旋羽根7のスムーズな回転を可能とし、かつ粒状固形物の移送途中に懸濁液の一部が流下してある程度液切りされるように図っているが、粒状固形物の移送効率を極力低下させない程度の広さに設定している。   A clearance 11 having an appropriate width is secured between the outer peripheral edge of the spiral blade 7 and the inner wall of the casing 4. The presence of the clearance 11 enables the spiral blade 7 to rotate smoothly and is a granular solid. While a part of the suspension flows down and is drained to some extent during the transfer of the product, it is set to a size that does not reduce the transfer efficiency of the granular solid as much as possible.

また、前記螺旋羽根7のように、軸心部に羽根支持用の軸体を有さずかつ片持ち構造である上、一端を自由端とした片持ち構造の螺旋羽根において、他端の駆動軸側に移送物を引き寄せようと回転させた場合、自由端側では螺旋を解く方向へ回転させることになるため、羽根にはより高い強度が求められるが、前記螺旋羽根7の軸心中空部6に面する内周縁には、4乃至8本程度の丸鋼製の補強部材12を略等間隔にて、軸心方向へかつ螺旋羽根7の略全長に亘って固着しており、これによって羽根強度を充分に高めつつ、また軸体が無いことによって期待できる大幅な軽量化とも併せて、粒状固形物移送時のように螺旋羽根7に大きな負荷が掛かった場合でも螺旋羽根7に湾曲や変形等が生じないように図っている。   Further, unlike the spiral blade 7, the shaft center portion does not have a blade support shaft and has a cantilever structure, and the other end is driven in a cantilever structure with one end being a free end. When the transported object is rotated toward the shaft side, it is rotated in the direction of unwinding the spiral on the free end side, so that higher strength is required for the blade, but the axial hollow portion of the spiral blade 7 6 to 8 round steel reinforcing members 12 are fixed at substantially equal intervals in the axial direction and over substantially the entire length of the spiral blade 7. While the blade strength is sufficiently increased and the significant weight reduction expected due to the absence of the shaft body, even when a large load is applied to the spiral blade 7 as in the case of transferring the granular solid, It is intended to prevent deformation and the like.

そして、上記粒状固形物の移送装置1を使用して粒状固形物を含んだ懸濁液から粒状固形物を分離して移送するときには、先ず、貯留ホッパ5に懸濁液を投入して貯留させ、ホッパ底部に沈殿する粒状固形物を下位のケーシング4内に投入させる。こうして、ケーシング4内に投入された粒状固形物は、螺旋羽根7の回転駆動によりケーシング4内壁に沿って斜め上方向の排出口3側へと順次引き上げられて移送されていくが、その際、粒状固形物に随伴する多量の懸濁液は、その一部が螺旋羽根7外周縁とケーシング4内壁とのクリアランス11から、その残りが螺旋羽根7の軸心に沿って形成された比較的大径の中空部6からケーシング4下端側へと素早く流下して液切れされ、効果的に分離される。   When the granular solid material is separated and transferred from the suspension containing the granular solid material using the granular solid material transfer device 1, first, the suspension is put into the storage hopper 5 to be stored. The granular solid that settles at the bottom of the hopper is put into the lower casing 4. In this way, the granular solid charged in the casing 4 is sequentially lifted and transferred along the inner wall of the casing 4 to the side of the discharge port 3 obliquely upward by the rotational drive of the spiral blade 7, A large amount of the suspension accompanying the granular solid is relatively large in which a part thereof is formed from the clearance 11 between the outer peripheral edge of the spiral blade 7 and the inner wall of the casing 4 and the rest is formed along the axis of the spiral blade 7. It quickly flows down from the hollow portion 6 having a diameter to the lower end side of the casing 4 to be drained and effectively separated.

このとき、本移送装置1では、螺旋羽根7の下端部を自由端とした片持ち構造を採用しており、ケーシング4下端側には軸受部が存在しないため、従来装置が抱えるような、軸受部からの懸濁液の漏洩や懸濁液を原因とするベアリングの極端な損耗等といった問題は起こり得ず、メンテナンス面において極めて好適なものとしている。   At this time, the transfer device 1 adopts a cantilever structure in which the lower end portion of the spiral blade 7 is a free end, and there is no bearing portion on the lower end side of the casing 4. Problems such as leakage of the suspension from the part and extreme wear of the bearing caused by the suspension cannot occur, which is extremely suitable in terms of maintenance.

このように、懸濁液に含まれる粒状固形物を移送する移送装置として、軸心に沿って大きな中空部が形成されるリボン状の螺旋羽根を採用したので、粒状固形物の移送効率を極力低下させることなく軸心中空部から懸濁液を素早く流下させて液切れさせ、極めて効果的に分離できる。また、螺旋羽根の上端部のみを駆動軸に固着した片持ち構造としてケーシング下端側の軸受部を不要としたので、従来装置が抱える、軸受部からの懸濁液の漏洩やベアリングの極端な損耗等といった問題が起こり得ず、メンテナンス面において極めて好適なものとすることができる。   As described above, since the ribbon-shaped spiral blade in which a large hollow portion is formed along the axial center is adopted as a transfer device for transferring the granular solid contained in the suspension, the transfer efficiency of the granular solid is minimized. The suspension can be quickly flowed down from the hollow portion of the shaft center without being lowered, and can be separated extremely effectively. In addition, since the bearing part on the lower end side of the casing is not required as a cantilever structure in which only the upper end part of the spiral blade is fixed to the drive shaft, suspension leakage from the bearing part and extreme wear of the bearing that conventional devices have Etc. cannot occur, and it can be made extremely suitable in terms of maintenance.

なお、本移送装置では、粒状固形物を含んだ懸濁液から、粒状固形物と懸濁液の何れを回収する場合にも好適に採用できる。即ち、有用な粒状固形物から不要な懸濁液を極力液切りさせるように分離して、高純度の粒状固形物を回収することを主目的とすることも可能であるし、或いは有用な懸濁液から不要な粒状固形物だけを極力排出させるように分離して、高純度の懸濁液を回収することを主目的とすることも勿論可能である。   In addition, in this transfer apparatus, it can employ | adopt suitably also when collect | recovering either a granular solid and a suspension from the suspension containing a granular solid. That is, it is possible to separate unnecessary suspension from useful granular solids as much as possible, and to recover high-purity granular solids, or to use useful suspensions. Of course, it is possible to separate the unnecessary granular solids from the turbid liquid so as to be discharged as much as possible and to recover a high-purity suspension.

例えば、生石灰と消化水とを攪拌混合させて消化反応させることにより生成される懸濁液の消石灰スラリーから、粒状固形物である未反応残渣を排出させて分離して、高純度の有用な消石灰スラリーを回収する場合にも好適に採用できる。   For example, high-purity useful slaked lime is obtained by discharging and separating unreacted residues that are granular solids from a slaked lime slurry in a suspension produced by stirring and mixing quick lime and digested water. It can also be suitably employed when recovering the slurry.

本発明に係る粒状固形物の移送装置の一実施例を示す概略図である。It is the schematic which shows one Example of the transfer apparatus of the granular solid based on this invention.

符号の説明Explanation of symbols

1…移送装置 2…投入口
3…排出口 4…ケーシング
5…貯留ホッパ 6…中空部
7…螺旋羽根 9…駆動軸
11…補強部材
DESCRIPTION OF SYMBOLS 1 ... Transfer apparatus 2 ... Input port 3 ... Discharge port 4 ... Casing 5 ... Storage hopper 6 ... Hollow part 7 ... Spiral blade 9 ... Drive shaft 11 ... Reinforcement member

Claims (1)

粒状固形物を含む懸濁液から粒状固形物を分離して移送する粒状固形物の移送装置であって、一端部に投入口を他端部に排出口を備えた略円筒形状のケーシングを排出口側が高くなるように傾斜配置し、該ケーシングの投入口には懸濁液貯留用の貯留ホッパを連結すると共に、ケーシング内部には軸心に沿って中空部が形成されるリボン状螺旋羽根を内装し、該螺旋羽根の上端部はケーシング上端側より貫通させて回転自在に軸支した駆動軸に固着する一方、螺旋羽根の下端部は固着せずに自由端とし、かつ螺旋羽根の軸心中空部に面する内周縁には複数の補強部材を軸心と平行に螺旋羽根の略全長に亘って固着し、前記螺旋羽根の回転によって懸濁液に含まれる粒状固形物をケーシング上端の排出口側へ引き上げて移送するときには、粒状固形物に随伴する懸濁液を螺旋羽根の軸心中空部よりケーシング下端側へ流下させて分離するように構成したことを特徴とする粒状固形物の移送装置。   An apparatus for transferring granular solids, which separates and transfers granular solids from a suspension containing granular solids, and discharges a substantially cylindrical casing having an inlet at one end and an outlet at the other end. A sloping arrangement is provided so that the outlet side becomes higher, and a storage hopper for storing suspension is connected to the inlet of the casing. The upper end of the spiral blade is fixed to a drive shaft that is rotatably supported by penetrating from the upper end side of the casing, while the lower end of the spiral blade is not fixed and is a free end, and the axial center of the spiral blade A plurality of reinforcing members are fixed to the inner peripheral edge facing the hollow portion over the substantially entire length of the spiral blade in parallel with the axial center, and the particulate solid contained in the suspension is discharged from the upper end of the casing by the rotation of the spiral blade. When transported by lifting to the outlet side, granular Transfer device particulate solids characterized by being configured to separate the suspension associated to the shape was allowed to flow down from the shaft suicide empty portion of the spiral blade to the casing lower end.
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Cited By (4)

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Publication number Priority date Publication date Assignee Title
CN104555298A (en) * 2014-11-19 2015-04-29 西安近代化学研究所 Powder explosive weight-loss spiral feeding machine
CN105129343A (en) * 2015-07-15 2015-12-09 安徽正远包装科技有限公司 Elevating method for spiral elevator
JP2019064119A (en) * 2017-09-29 2019-04-25 株式会社カワタ Feeding device and measuring and mixing device
CN110027858A (en) * 2019-05-24 2019-07-19 襄阳汇博机械设备有限公司 A kind of screw conveyor

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JPS5968630U (en) * 1982-10-30 1984-05-09 マツダ株式会社 Wet sand recovery device
JPH01137397U (en) * 1988-03-08 1989-09-20
JPH09301517A (en) * 1996-05-15 1997-11-25 Sekisui Chem Co Ltd Screw for screw conveyor

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Publication number Priority date Publication date Assignee Title
JPS5968630U (en) * 1982-10-30 1984-05-09 マツダ株式会社 Wet sand recovery device
JPH01137397U (en) * 1988-03-08 1989-09-20
JPH09301517A (en) * 1996-05-15 1997-11-25 Sekisui Chem Co Ltd Screw for screw conveyor

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104555298A (en) * 2014-11-19 2015-04-29 西安近代化学研究所 Powder explosive weight-loss spiral feeding machine
CN105129343A (en) * 2015-07-15 2015-12-09 安徽正远包装科技有限公司 Elevating method for spiral elevator
JP2019064119A (en) * 2017-09-29 2019-04-25 株式会社カワタ Feeding device and measuring and mixing device
JP6994233B2 (en) 2017-09-29 2022-01-14 株式会社カワタ Feeder and metering mixer
CN110027858A (en) * 2019-05-24 2019-07-19 襄阳汇博机械设备有限公司 A kind of screw conveyor

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