JPH06344190A - Filter - Google Patents
FilterInfo
- Publication number
- JPH06344190A JPH06344190A JP5134470A JP13447093A JPH06344190A JP H06344190 A JPH06344190 A JP H06344190A JP 5134470 A JP5134470 A JP 5134470A JP 13447093 A JP13447093 A JP 13447093A JP H06344190 A JPH06344190 A JP H06344190A
- Authority
- JP
- Japan
- Prior art keywords
- filtered
- filter
- coil spring
- filter medium
- gap
- 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.)
- Granted
Links
- 239000012065 filter cake Substances 0.000 claims abstract description 16
- 239000000706 filtrate Substances 0.000 claims abstract description 16
- 239000000126 substance Substances 0.000 claims description 5
- 238000012546 transfer Methods 0.000 claims description 4
- 239000007787 solid Substances 0.000 abstract description 14
- 239000007788 liquid Substances 0.000 abstract description 6
- 238000001914 filtration Methods 0.000 description 9
- 239000000463 material Substances 0.000 description 7
- 230000002093 peripheral effect Effects 0.000 description 5
- 238000000926 separation method Methods 0.000 description 4
- 239000013013 elastic material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 238000011056 performance test Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910000639 Spring steel Inorganic materials 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000010840 domestic wastewater Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、液体と固体の混合体
を、所定の大きさ以上の固体の濾塊と濾過によって濾さ
れた濾液とに分離する濾過機に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a filter for separating a mixture of liquid and solid into a filter cake of solid having a predetermined size or more and a filtrate filtered by filtration.
【0002】[0002]
【従来の技術】一般に、スラリまたは泥漿(スラッジ)
と称される液体と固体との混合物からなる被濾過体を、
所定の大きさ以上の固体の濾塊と、濾過によって濾され
た濾液とに分離する各種の濾過機が、生活排水または各
種の産業排水の分離処理等に多用されている。BACKGROUND OF THE INVENTION Generally, a slurry or sludge.
The object to be filtered consisting of a mixture of liquid and solid called
Various filters for separating a solid filter cake of a predetermined size or more and a filtrate filtered by filtration are frequently used for separation treatment of domestic wastewater or various industrial wastewater.
【0003】以下、従来の各種の濾過機について説明す
る。Various conventional filters will be described below.
【0004】従来の濾過機の一例としていわゆるスクリ
ュープレスと称されるものが知られている。このスクリ
ュープレスは、適宜な大きさの多数の貫通孔を有するパ
ンチングメタル等により円筒形状の篩面とされた濾材を
形成するとともに、この濾材の内部に適宜なスパイラル
コンベアを配設したものであり、濾材の内部に投入され
た被濾過体をスパイラルコンベアをもって移送しながら
連続的に圧縮することにより、被濾過体を篩面をもって
所定の大きさ以上の固体の濾塊と、濾過によって濾され
た濾液とに分離(固液分離)するようにされている。A so-called screw press is known as an example of a conventional filter. This screw press is one in which a filter material having a cylindrical sieve surface is formed by punching metal or the like having a large number of through holes of an appropriate size, and an appropriate spiral conveyor is disposed inside the filter material. The object to be filtered put into the inside of the filter medium is continuously compressed while being transferred by a spiral conveyer, and the object to be filtered is filtered by a solid filter cake of a predetermined size or more with a sieve surface and filtered. It is designed to be separated into a filtrate (solid-liquid separation).
【0005】従来の濾過機の他の例として多重円盤型の
ものが知られている。この多重円盤型の濾過機は、多数
の薄片の円板を積層して濾材を形成し、被濾過体を多数
の薄片の円板の間隔(隙間)をもって所定の大きさ以上
の固体の濾塊と、濾過によって濾された濾液とに分離
(固液分離)するようにされている。As another example of the conventional filter, a multi-disk type is known. This multi-disc type filter is formed by laminating a large number of thin discs to form a filter medium, and the object to be filtered is a solid filter cake of a predetermined size or more with a space (gap) between the thin discs. And a filtrate filtered by filtration (solid-liquid separation).
【0006】従来の濾過機のさらに他の例として渦巻ス
クリュー型のものが知られている。この渦巻スクリュー
型の濾過機は、遊動リングと固定リングとを交互に組み
合わせた円筒型濾材を形成するとともに、この濾材の内
部に適宜なスパイラルコンベアを配設したものであり、
濾材の内部に投入された被濾過体をスパイラルコンベア
をもって移送しながら、被濾過体を遊動リングと固定リ
ングとの隙間(間隔)をもって所定の大きさ以上の固体
の濾塊と、濾過によって濾された濾液とに分離(固液分
離)するようにされている。As another example of the conventional filter, a spiral screw type is known. This spiral screw type filter is one in which a floating ring and a fixed ring are alternately combined to form a cylindrical filter medium, and an appropriate spiral conveyor is disposed inside the filter medium,
While the object to be filtered put into the inside of the filter medium is transferred by the spiral conveyor, the object to be filtered is filtered by filtration with a solid filter lump of a predetermined size or more with a gap (spacing) between the floating ring and the fixed ring. And the filtrate is separated (solid-liquid separation).
【0007】[0007]
【発明が解決しようとする課題】しかしながら、前述し
た従来の何れの濾過機においても、被濾過体を固体の濾
塊と濾過によって濾された濾液とに分離することはでき
るものの、被濾過体の濾塊の大きさが変動する場合や、
1日の中で午前と午後において異なる被濾過体を濾過す
る場合や、季節によって異なる被濾過体を濾過する場合
等に、濾過機の濾材を交換することができないために、
被濾過体から分離する固体の大きさを変えることができ
ず、このため被濾過体から分離する固体の大きさの異な
る濾材を有する複数の濾過機を用いるか、あるいは濾過
性能を犠牲にするしかないという問題点があった。However, in any of the above-mentioned conventional filters, although the substance to be filtered can be separated into a solid filter cake and a filtrate filtered by filtration, If the size of the filter cake changes,
Since it is not possible to replace the filter material of the filter when filtering different objects to be filtered in the morning and afternoon in the day, or when filtering different objects to be filtered depending on the season,
It is not possible to change the size of the solids separated from the object to be filtered, and therefore, it is necessary to use a plurality of filters having filter media having different sizes of the solids to be separated from the object to be filtered, or to sacrifice the filtering performance. There was a problem that it did not exist.
【0008】また、客先にて濾過機のデモンストレーシ
ョンまたは性能テスト等を行う場合に、予め多数のテス
ト機(濾過機)を用意するのは、保管スペースや経済的
負担が重くて不可能なため、限られた台数、通常は1台
の濾過機をもって、不特定多数の種類の被濾過体に対し
てデモンストレーションまたは性能テスト等を行わざる
を得ず、前述したように濾過機の濾材を交換することが
できないために、被濾過体とテスト機の濾材とを最適な
状態に対応させることが困難であり、濾過機本来の性能
を発揮させることができないという問題点があった。[0008] In addition, it is impossible to prepare a large number of testers (filters) in advance when performing a demonstration or a performance test of the filters at the customer site because the storage space and the economic burden are heavy. However, with a limited number of filters, usually one filter, there is no choice but to carry out a demonstration or performance test on an unspecified number of types of objects to be filtered, and the filter material of the filter is replaced as described above. Since it is not possible, it is difficult to make the filter medium of the tester and the filter material of the tester correspond to the optimum state, and there is a problem that the original performance of the filter cannot be exhibited.
【0009】本発明は、前述した従来のものにおける問
題点を克服し、多種多様の被濾過体に一つの濾材をもっ
て対応することのできる濾過機を提供することを目的と
する。It is an object of the present invention to provide a filter that overcomes the above-mentioned problems of the conventional one and can handle a wide variety of objects to be filtered with a single filter material.
【0010】[0010]
【課題を解決するための手段】前述した目的を達成する
ため本発明の濾過機は、被濾過体を濾塊と濾液とに分離
させる略円筒形状のコイルばねからなる濾材と、前記コ
イルばねの間隔を調節自在とする調節手段と、前記濾材
の内部に投入された被濾過体を加圧移動させる移送手段
とを有することを特徴としている。In order to achieve the above-mentioned object, a filter according to the present invention comprises a filter medium composed of a coil spring having a substantially cylindrical shape for separating a filter body into a filter cake and a filtrate, and It is characterized in that it has an adjusting means for making the interval adjustable and a transferring means for moving the object to be filtered introduced into the inside of the filter medium under pressure.
【0011】[0011]
【作用】前述した構成からなる本発明の濾過機によれ
ば、コイルばねからなる濾材の間隔を調節自在とするこ
とができるので、一つの濾材をもって多種多様の被濾過
体を最適な状態で分離することができる。According to the filter of the present invention having the above-mentioned structure, the interval of the filter medium composed of the coil spring can be adjusted freely, so that one filter medium can be used to optimally separate a wide variety of objects to be filtered. can do.
【0012】[0012]
【実施例】以下、本発明の実施例を図面について説明す
る。Embodiments of the present invention will now be described with reference to the drawings.
【0013】図1は本発明の濾過機の一実施例の要部の
構成を示す概略図であり、図2はコイルばねの断面形状
の適用例を示す断面図である。FIG. 1 is a schematic view showing the structure of the essential part of an embodiment of the filter of the present invention, and FIG. 2 is a cross-sectional view showing an application example of the cross-sectional shape of a coil spring.
【0014】図1に示すように、本実施例の濾過機1に
は、濾材2として断面略四角形状の弾性素材を所望の間
隔(隙間)G(図において誇張して示す)をもって螺旋
状に形成し、全体として略円筒形状に形成されたコイル
ばね3を有している。このコイルばね3は、図において
左方に示す適宜な調節手段4により、軸方向に伸縮自在
とされている。すなわち、コイルばね3の間隔Gが調節
自在とされている。なお、前記調節手段4の一例として
は、コイルばね3の一端をねじ軸に螺合しているナット
に固定し、ねじ軸を回転してねじ軸の軸方向におけるナ
ットの位置を変化させることによりコイルばね3の間隔
Gを調節しうるようにすることができるが、コイルばね
3の間隔Gを調節できるものであればこのような構成に
限定されるものではない。As shown in FIG. 1, in the filter 1 of this embodiment, an elastic material having a substantially quadrangular cross section is used as a filter medium 2 in a spiral shape with a desired gap (gap) G (exaggerated in the figure). The coil spring 3 is formed and has a substantially cylindrical shape as a whole. The coil spring 3 can be expanded and contracted in the axial direction by an appropriate adjusting means 4 shown on the left side of the drawing. That is, the distance G between the coil springs 3 is adjustable. As an example of the adjusting means 4, one end of the coil spring 3 is fixed to a nut screwed to a screw shaft, and the screw shaft is rotated to change the position of the nut in the axial direction of the screw shaft. The distance G between the coil springs 3 can be adjusted, but the invention is not limited to such a structure as long as the distance G between the coil springs 3 can be adjusted.
【0015】また、コイルばね3の間隔Gを間歇的に拡
開して目詰まりを防止する目詰まり防止手段が設けられ
ている。この目詰まり防止手段としては、特願平4−2
72852号に記載の構成があるが、この先願の構成に
限定されるものではない。また、間隔Gの間歇的な拡開
に加えて振動を加えたりあるいは洗浄するようにしても
よい。There is also provided a clogging prevention means for intermittently expanding the gap G between the coil springs 3 to prevent clogging. As a means for preventing this clogging, Japanese Patent Application No. 4-2 is used.
Although there is a structure described in Japanese Patent No. 72852, it is not limited to the structure of this prior application. Further, in addition to intermittently expanding the gap G, vibration may be applied or cleaning may be performed.
【0016】一方、前記コイルばね3の素材としては、
ステンレス、アルミニウム、ばね鋼、樹脂等の各種弾性
素材から、濾過機1の設計コンセプトにより選択して用
いればよい。On the other hand, as the material of the coil spring 3,
It may be selected from various elastic materials such as stainless steel, aluminum, spring steel, and resin according to the design concept of the filter 1.
【0017】そして、前記コイルばね3の断面形状は、
コイルばね3の少なくとも内周面を平滑に形成できる形
状、例えば、図2のaに示す断面矩形、図2のbに示す
断面逆三角形、図2のcに示す外周側が内周側より短い
断面台形、図2のdに示す断面円形等を用いてもよく、
特に、本実施例に限定されるものではない。The cross-sectional shape of the coil spring 3 is
A shape that allows at least the inner peripheral surface of the coil spring 3 to be formed smoothly, for example, a rectangular cross section shown in FIG. 2A, an inverted triangular cross section shown in FIG. 2B, and a cross section in which the outer peripheral side shown in FIG. 2C is shorter than the inner peripheral side. A trapezoid, a circular cross section shown in d of FIG. 2 or the like may be used,
In particular, it is not limited to this embodiment.
【0018】図1に戻って、前記コイルばね3の内部に
は、被濾過体Sを図において右方から左方に移送しなが
ら徐々に加圧する(加圧移送)移送手段5として、適宜
なスパイラルコンベア5aが、その両端をコイルばね3
の両端から突出するようにして回転自在に配設されてい
る。このスパイラルコンベア5aは、図示しない駆動モ
ータ等の適宜な駆動源により駆動されるようになってい
る。Returning to FIG. 1, inside the coil spring 3, there is an appropriate transfer means 5 for gradually pressurizing the object S to be filtered while transferring it from the right side to the left side in the figure (pressurized transfer). The spiral conveyor 5a has coil springs 3 at both ends.
Are rotatably arranged so as to project from both ends of the. The spiral conveyor 5a is driven by an appropriate drive source such as a drive motor (not shown).
【0019】前記コイルばね3の図において右端には、
被濾過体Sが投入される適宜な投入ホッパ6が配設され
ており、前記調節手段4の図において左端には、脱水ケ
ーキと称される脱水された濾塊Kを排出する適宜な排出
ホッパ7が配設されている。また、前記コイルばね3の
下方には、適宜な濾液槽8が配設されている。At the right end of the coil spring 3 in the drawing,
An appropriate input hopper 6 into which the substance to be filtered S is input is provided, and an appropriate output hopper for discharging the dehydrated filter cake K called a dehydrated cake is provided at the left end of the adjusting means 4 in the drawing. 7 are provided. An appropriate filtrate tank 8 is arranged below the coil spring 3.
【0020】つぎに、前述した構成からなる本実施例の
作用について説明する。Next, the operation of this embodiment having the above-mentioned structure will be described.
【0021】図1に示すように、本実施例の濾過機1を
稼動させると、図示しない駆動モータの駆動力によりス
パイラルコンベア5aが所望の回転速度をもって回転を
開始する。そして、図中右側の投入ホッパ6の上部から
所望の被濾過体Sを供給する。すると、被濾過体Sは、
調節手段4をもって、被濾過体Sの固体の大きさに対応
させて間隔Gを調節されたコイルばね3の内部を、スパ
イラルコンベア5aの表面に沿って、図において右方か
ら左方に移送されながら徐々に加圧され(加圧移動)て
通過する途中で、所定の大きさの濾塊Kと濾過された濾
液Eとに分離されるとともに、濾塊Kは徐々に圧縮され
つつ脱水されて、脱水ケーキと称される脱水された濾塊
Kとなって排出ホッパ7から排出される。また、コイル
ばね3により濾過(分離)された濾液Eならびに濾塊K
から脱水された水分Eaは、コイルばね3の隙間Gを介
してコイルばね3の内部から表面に向かって通過した
後、コイルばね3の下方に配設された所望の濾液槽8内
に貯留される。As shown in FIG. 1, when the filter 1 of this embodiment is operated, the spiral conveyor 5a starts to rotate at a desired rotation speed by the driving force of a drive motor (not shown). Then, the desired object S to be filtered is supplied from the upper part of the charging hopper 6 on the right side in the figure. Then, the object S to be filtered is
With the adjusting means 4, the inside of the coil spring 3 whose gap G is adjusted according to the size of the solid of the body S to be filtered is transferred from right to left in the figure along the surface of the spiral conveyor 5a. While being gradually pressurized (pressurized movement) and passing through, it is separated into a filter cake K having a predetermined size and a filtrate E filtered, and the filter cake K is gradually compressed and dehydrated. Dehydrated cake K called a dehydrated cake is discharged from the discharge hopper 7. Also, the filtrate E and the filter cake K filtered (separated) by the coil spring 3
The water Ea dehydrated from the water passes through the gap G of the coil spring 3 from the inside of the coil spring 3 toward the surface, and then is stored in a desired filtrate tank 8 arranged below the coil spring 3. It
【0022】また、本実施例のコイルばね3の少なくと
も内周面は平滑に形成されているので、コイルばね3の
内周面に当接する被濾過体Sおよび濾塊Kを、円滑に移
送することができる。Further, since at least the inner peripheral surface of the coil spring 3 of the present embodiment is formed to be smooth, the body S to be filtered and the filter cake K which come into contact with the inner peripheral surface of the coil spring 3 are transferred smoothly. be able to.
【0023】したがって、本発明の濾過方法を適用する
本実施例の濾過機1によれば、従来と異なり、被濾過体
Sに含有されている固体の大きさに対応させて、コイル
ばね3の間隔Gを調節自在(可変)とすることができる
ので、被濾過体Sを確実に濾過(分離)することができ
るとともに、一つの濾材2を多種多様の被濾過体Sに対
して最適化させることができる。Therefore, according to the filter 1 of the present embodiment to which the filtering method of the present invention is applied, unlike the prior art, the coil spring 3 of the coil spring 3 is made to correspond to the size of the solid contained in the body S to be filtered. Since the interval G can be adjusted (variable), the object S to be filtered can be reliably filtered (separated), and one filter medium 2 is optimized for a wide variety of objects S to be filtered. be able to.
【0024】なお、調節手段4によるコイルばね3の間
隔Gの調節は、被濾過体Sに対応させて予め調節して
も、濾過機1を稼動させた状態で調節しても、どちらで
もよく、使用状況により選択することができる。It should be noted that the adjustment of the gap G between the coil springs 3 by the adjusting means 4 may be carried out in advance according to the object S to be filtered, or while the filter 1 is in operation. , It can be selected according to the usage situation.
【0025】また、本発明は、前記実施例に限定される
ものではなく、必要に応じて変更することができる。Further, the present invention is not limited to the above-mentioned embodiment, but can be modified as necessary.
【0026】[0026]
【発明の効果】以上説明したように本発明の濾過機によ
れば、被濾過体を濾塊と濾液とに確実に分離することが
できるとともに、一つの濾材をもって多種多様の被濾過
体に用いることができるという極めて優れた効果を奏す
る。As described above, according to the filter of the present invention, the substance to be filtered can be surely separated into the filter cake and the filtrate, and one filter medium is used for a wide variety of substances to be filtered. It has an extremely excellent effect of being able to.
【図1】本発明に係る濾過機の一実施例の要部の構成を
示す概略図FIG. 1 is a schematic diagram showing a configuration of a main part of an embodiment of a filter according to the present invention.
【図2】aからdはコイルばねの断面形状の適用例を示
す断面図2A to 2D are cross-sectional views showing an application example of a cross-sectional shape of a coil spring.
1 濾過機 2 濾材 3 コイルばね 4 調節手段 5 移送手段 5a スパイラルコンベア 6 投入ホッパ 7 排出ホッパ 8 濾液槽 E 濾液 Ea 水分 G 間隔(隙間) K 濾塊 S 被濾過体 1 Filter 2 Filter medium 3 Coil spring 4 Adjusting means 5 Transfer means 5a Spiral conveyor 6 Input hopper 7 Discharge hopper 8 Filtrate tank E Filtrate Ea Moisture G Interval (gap) K Filter mass S Filtered body
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 B01D 29/48 7112−4D (72)発明者 石橋 勝嘉 東京都羽村市緑ケ丘3丁目6番5号 株式 会社柳河技研開発本部内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification number Reference number within the agency FI Technical indication location B01D 29/48 7112-4D (72) Inventor Katsuyoshi Ishibashi 3-6-5 Midorigaoka, Hamura-shi, Tokyo No. Stock Company Yanagawa Giken Development Division
Claims (1)
円筒形状のコイルばねからなる濾材と、前記コイルばね
の間隔を調節自在とする調節手段と、前記濾材の内部に
投入された被濾過体を加圧移動させる移送手段とを有す
ることを特徴とする濾過機。1. A filter medium composed of a substantially cylindrical coil spring for separating a substance to be filtered into a filter cake and a filtrate, an adjusting means for adjusting an interval between the coil springs, and a filter medium charged inside the filter medium. And a transfer means for moving the object to be filtered under pressure.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5134470A JPH0798276B2 (en) | 1993-06-04 | 1993-06-04 | Filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5134470A JPH0798276B2 (en) | 1993-06-04 | 1993-06-04 | Filter |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH06344190A true JPH06344190A (en) | 1994-12-20 |
| JPH0798276B2 JPH0798276B2 (en) | 1995-10-25 |
Family
ID=15129077
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP5134470A Expired - Fee Related JPH0798276B2 (en) | 1993-06-04 | 1993-06-04 | Filter |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0798276B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104210129A (en) * | 2014-08-30 | 2014-12-17 | 蒋世芬 | Small hand peanut oil press |
| CN113277700A (en) * | 2021-06-07 | 2021-08-20 | 黔南高新区绿色化工技术研究院有限公司 | Solid-liquid separation system of aquaculture wastewater ammonia nitrogen treatment system |
-
1993
- 1993-06-04 JP JP5134470A patent/JPH0798276B2/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104210129A (en) * | 2014-08-30 | 2014-12-17 | 蒋世芬 | Small hand peanut oil press |
| CN113277700A (en) * | 2021-06-07 | 2021-08-20 | 黔南高新区绿色化工技术研究院有限公司 | Solid-liquid separation system of aquaculture wastewater ammonia nitrogen treatment system |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0798276B2 (en) | 1995-10-25 |
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