JP3781253B2 - Disc filter filter media - Google Patents

Disc filter filter media Download PDF

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Publication number
JP3781253B2
JP3781253B2 JP25265299A JP25265299A JP3781253B2 JP 3781253 B2 JP3781253 B2 JP 3781253B2 JP 25265299 A JP25265299 A JP 25265299A JP 25265299 A JP25265299 A JP 25265299A JP 3781253 B2 JP3781253 B2 JP 3781253B2
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JP
Japan
Prior art keywords
filter
wedge wire
drive shaft
chamber
filter medium
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.)
Expired - Fee Related
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JP25265299A
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Japanese (ja)
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JP2001070718A (en
Inventor
邦夫 藤田
政文 那須
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Ishigaki Co Ltd
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Ishigaki Co Ltd
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Priority to JP25265299A priority Critical patent/JP3781253B2/en
Publication of JP2001070718A publication Critical patent/JP2001070718A/en
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Publication of JP3781253B2 publication Critical patent/JP3781253B2/en
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  • Filtration Of Liquid (AREA)

Description

【0001】
【発明の属する技術分野】
この発明は、下水汚泥などの難ろ過性汚泥のろ過機のろ材に関し、特に、ろ過室にインペラーを配設した円盤ろ過機のろ材の改良に関する。
【0002】
【従来の技術】
従来、円盤ろ過機のろ材としては、目抜き板に補強を施した円盤枠内に直径0.25mmから0.5mmの穴を有する薄いパンチングメタルを取り付けていた。また、脱水機に使用するろ材としては、例えば、特開平6−233906号公報に記載してあるように、表面が平坦で断面が一定形状のフイルター用線材を非角形版状体に固着し、直線状のスリットを多数形成したろ材は公知である。また、特開平6−210114号公報に記載してあるように、ウエッジワイヤーを並行して各ワイヤー間にV型開口の連続スリットを形成したウエッジワイヤースクリーンもよく知られている。
【0003】
【発明が解決しようとする課題】
しかしながら、このような従来の金属ろ材では、下水汚泥などの濃縮された汚泥をポリマーで凝縮させてろ過した場合、ろ材の穴から抜けた一部の固形物が補強円盤枠に残り、ろ液の流れが悪くなり、ろ過に支障があり、ろ材の洗浄頻度が多くなっていた。また、このような金属ろ材では、強度不足で高圧搾圧力をかけられない上、無機質を含む汚泥を圧搾する場合には、すぐ摩耗して破損する。しかも、破損した場合のろ材交換には多大な手間と時間を要する難点があった。
【0004】
【課題を解決するための手段】
この発明は、上記の課題を解決することを目的とするものであって、2枚の円盤状のろ過板と外周環と一対の内環支持筒とでろ過室を形成し、前記内環支持筒には支持筒を連結し、該支持筒に駆動軸を内挿し、前記駆動軸の内部に原液の供給路を設け、前記駆動軸の周面に複数の供給口を開口して、ろ過室に連通させると共に、ろ過室に回転自在な羽根車を配設し、前記ろ過室に原液を圧入供給するろ過機において、上記ろ過板はウエッジワイヤースクリーンと放射状リブを有する円環支持枠を接合一体化した金属円盤ろ材である。そして、ウエッジワイヤースクリーンは水平状に並列したウエッジワイヤーとこのウエッジワイヤーを固定するための垂直方向に並列したサポートロッドから構成されており、ウエッジワイヤースクリーンの目開きが100μmから200μmの範囲に設けてある。
【0005】
【発明の実施の形態】
この発明に係る円盤ろ過機のろ材は上記のように構成してあり、ろ過室を形成するろ過板をウエッジワイヤースクリーンと放射状リブを有する円環支持枠を接合一体化することにより、強度が増し高圧搾圧力に対しても破損がなく、低含水率のケーキが得られるものである。そして、ろ材の取付けが容易となり、維持管理上都合がよいものである。また、ウエッジワイヤースクリーンはウエッジワイヤーを水平状に並列し、ウエッジワイヤーを固定するサポートロッドを垂直方向に並列したのでろ液と一部固形物の溜りが少なくなり、ろ材洗浄頻度が少なくてすむものである。
【0006】
【実施例】
この発明に係る円盤ろ過機のろ材を図面に基づき詳述すると、まず、図1及び図2において、符号1は一対の金属円盤ろ材からなるろ過板であって、このろ過板1は横方向に多数並列したウエッジワイヤー2…に裏面から縦方向に多数のサポートロッド3…を止着したウエッジワイヤースクリーン4と放射状リブ5を有する円環支持枠6を接合一体化した構造となっている。ウエッジワイヤー2の横方向のスリットの目にろ液と一緒に目抜けした固形物が、裏側のサポートロッド3の縦方向のスリットの目に沿って流下するろ液で洗い流すようにしてあり、スリットの目にろ液と固形物の溜まりがなく、ろ材洗浄頻度が減少するようにしてある。この一対のろ過板1、1は、図3に示すように、その外周端が外周環7に連結され、その内周外壁が一対の内環支持筒8、8に連結されて円環状のろ過室9を構成してあり、ろ過板1の取付け、取り外しを容易にしてある。
【0007】
内環支持筒8には支持筒10が連結してあり、図4に示すように、ろ過室9の前後の支持筒10、10が軸受11、11を介してフレーム12、12に支架してある。支持筒10の内部には駆動軸13が挿通してあり駆動軸13の一端に嵌着した駆動プーリー14が駆動機15に連動連結してある。そして、駆動軸13の内部には原液の供給路16が設けてあり、ろ過室9に連通する複数の供給口17…が駆動軸13の周面に開口してある。ろ過室9と駆動軸13の間には内環支持筒8と支持筒10で囲まれた原液供給室18が形成されている。駆動軸13の一端には自在継手19を介して原液の供給管20が接続してあり、供給管20は供給ポンプ21を介して汚泥タンク22に連結してあり、汚泥タンク22に貯溜してある汚泥を駆動軸13の複数の供給口17…から原液供給室18に流入させ、原液供給室18からろ過室9に汚泥を均等に圧入するようにしてある。
【0008】
ろ過室9には図3及び図5に示すように、支持筒10の内部に挿通した駆動軸13に羽根車23が支架してあり、羽根車23の側縁をろ過板1に近接させ、その先端部を回転方向後方に後退させてある。駆動機15を作動して羽根車23をろ過室9内で回転させるようにしてある。この発明の実施例にあっては、羽根車23の羽根23aが4個の直片に折り曲げて湾曲線に近似させてあり、羽根枚数を6枚とした羽根車23をろ過室9内に配設してある。このように、羽根23aを直片に折り曲げて湾曲線に近似させれば、製作が容易となるものである。そして、羽根車23の回転方向背面の羽根23aにはその羽根面の中心部に沿って垂直に補強板24が止着してある。この補強板24は羽根23aの回転方向背面に配設した補強用のリブとして、ボス23b側から羽根23aの先端に向ってその高さが漸次低くなるようにしてあり、補強効果とともに供回り作用を最小限に押える形状としてある。
【0009】
ろ過室9の周部の外周環7には、図6に示すように、ケーキの取出口25が設けてあり、取出口25に配設した背圧調整弁26をシリンダー27を操作して、ろ過室9に背圧を加えるようにしてある。なお、符号28は取出口25に設けたケーキシュート、符号29はろ液受トラフ、符号30はろ過板1の洗浄管、符号31は洗浄水等の飛散防止カバーである。
【0010】
この発明に係る装置は、上記のように構成してあり、ろ過板1のウエッジワイヤースクリーン4の目開きを100μmから200μmの範囲に設定して、羽根車23を0.1〜1.0rpmで微速回転させながら、駆動軸13の供給路16からろ過室9の中心部分に0.1〜0.7Kg/cm2の圧入圧で汚泥を供給すると、汚泥の押込圧力と羽根車23の回転による押圧力を受けて外周方向に向って加圧搬送され、その左右のろ過板1のウエッジワイヤースクリーン4により水分が分離される。圧入直後の軸心部近傍では、主に圧入圧力で汚泥は濃縮され、羽根車23はその濃縮された汚泥とろ過板1との摺動摩擦抵抗力に打ち勝つ力で汚泥を押圧し、汚泥は圧入圧力と羽根23aの回転作用力により湾曲移動するケーキにせん断作用が加えられる。そして、取出口25の背圧調整弁26で背圧を加えながら脱水ケーキを取出すことができ、羽根車23の羽根23aの側面がろ過板1の内面に接近して回転するので、ろ過板1が目詰まりすることがなく、連続運転が可能となるものである。ポリマーで凝集した下水混合生汚泥(固形物濃度1.59%W/V)で脱水試験を実施した結果はケーキ含水率78.7%、SS回収率98.1%と良好なものであった。即ち、原液の圧入圧と羽根車の回転速度からウエッジワイヤースクリーン4の目開きを、100μmから200μmの範囲に設定すれば、含水率の少ないケーキと固形分の目抜けの少ないろ液が得られるものである。
【0011】
【発明の効果】
以上の説明で明らかなように、この発明に係る円盤ろ過機のろ材は上記のように構成してあり、ろ過板がウエッジワイヤースクリーンと放射状リブを有する円環支持枠を接合一体化した金属円盤ろ材としてあるので、強度が増し高圧搾圧力に対しても破損がなくろ過板の取付け、取り外しも容易となるものである。そして、ウエッジワイヤースクリーンは水平状に並列したウエッジワイヤーとこのウエッジワイヤーを固定するための垂直方向に並列したサポートロッドで構成してあるので、ウエッジワイヤーのスリットの目にろ液と一緒に目抜けした固形物が裏側のサポートロッドのスリットの目に沿って流下するろ液で洗い流されるので、スリットの目にろ液と固形物の溜まりがなく、ろ材洗浄頻度も減少するものである。
【図面の簡単な説明】
【図1】 ウエッジワイヤースクリーンの正面図である。
【図2】 ウエッジワイヤースクリーンを円環支持枠に嵌入したろ過板の裏面図である。
【図3】 この発明に係るろ過室を駆動軸に保持させた要部縦断側面図である。
【図4】 この発明に係るろ材を用いた円盤ろ過機の縦断側面図である。
【図5】 円盤ろ過機に配設した羽根車の正面図である。
【図6】 この発明に係るろ材を用いた円盤ろ過機の縦断正面図である。
【符号の説明】
1 ろ過板
2 ウェッジワイヤー
3 サポートロッド
4 ウエッジワイヤースクリーン
5 放射状リブ
6 円環支持枠
7 外周環
9 ろ過室
23 羽根車
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a filter medium for a filter of difficult-to-filter sludge such as sewage sludge, and particularly to an improvement of a filter medium of a disk filter having an impeller disposed in a filter chamber.
[0002]
[Prior art]
Conventionally, as a filter medium of a disk filter, a thin punching metal having a hole having a diameter of 0.25 mm to 0.5 mm is attached in a disk frame in which a cutout plate is reinforced. Further, as a filter medium used in a dehydrator, for example, as described in JP-A-6-233906, a filter wire having a flat surface and a constant cross section is fixed to a non-square plate-like body, Filter media having a large number of straight slits are known. Further, as described in JP-A-6-210114, a wedge wire screen is also well known in which wedge wires are arranged in parallel and a continuous slit having a V-shaped opening is formed between the wires.
[0003]
[Problems to be solved by the invention]
However, in such a conventional metal filter medium, when concentrated sludge such as sewage sludge is condensed with a polymer and filtered, some solid matter that has come out of the hole in the filter medium remains in the reinforcing disk frame, and the filtrate The flow became worse, the filtration was hindered, and the frequency of washing the filter media was increased. Moreover, in such a metal filter medium, high pressure cannot be applied due to insufficient strength, and when squeezing sludge containing inorganic matter, it is worn out and damaged immediately. In addition, there has been a problem that replacing the filter medium in the case of breakage requires a lot of labor and time.
[0004]
[Means for Solving the Problems]
The present invention aims to solve the above-mentioned problem, and forms a filtration chamber with two disc-shaped filter plates, an outer ring and a pair of inner ring support cylinders, and supports the inner ring. A support cylinder is connected to the cylinder, a drive shaft is inserted into the support cylinder, a supply path for the stock solution is provided inside the drive shaft, and a plurality of supply ports are opened on the peripheral surface of the drive shaft, and a filtration chamber together to communicate with the, disposed a rotatable impeller filtration chamber, wherein in the filtration machine for press-fitting supplying stock to the filtering chamber, the filter plate is joined integrally an annular support frame having a wedge wire screen and the radial rib This is a metal disk filter material. The wedge wire screen is composed of wedge wires arranged in parallel horizontally and support rods arranged in parallel in the vertical direction for fixing the wedge wires, and the opening of the wedge wire screen is provided in the range of 100 μm to 200 μm. is there.
[0005]
DETAILED DESCRIPTION OF THE INVENTION
The filter medium of the disk filter according to the present invention is configured as described above, and the strength is increased by joining and integrating the wedge plate and the annular support frame having the radial ribs to the filter plate forming the filter chamber. There is no breakage against high pressure and a cake with a low water content can be obtained. And attachment of a filter medium becomes easy and it is convenient on maintenance. In addition, the wedge wire screen has the wedge wires arranged in parallel horizontally and the support rods fixing the wedge wires arranged in parallel in the vertical direction, so that there is less accumulation of filtrate and some solid matter, and the frequency of washing the filter media can be reduced. .
[0006]
【Example】
The filter medium of the disk filter according to the present invention will be described in detail with reference to the drawings. First, in FIGS. 1 and 2, reference numeral 1 is a filter plate made of a pair of metal disk filter media. A wedge wire screen 4 in which a large number of support rods 3 are fixed in the longitudinal direction from the back surface and a circular support frame 6 having radial ribs 5 are joined and integrated with a large number of parallel wedge wires 2. The solid matter that has gotten through with the filtrate in the lateral slits of the wedge wire 2 is washed away with the filtrate that flows down along the longitudinal slits of the support rod 3 on the back side. There is no accumulation of filtrate and solid matter in the eyes, and the frequency of filter media washing is reduced. As shown in FIG. 3, the pair of filter plates 1, 1 has an outer peripheral end connected to the outer ring 7, and an inner peripheral outer wall connected to the pair of inner ring support cylinders 8, 8. The chamber 9 is configured to facilitate the attachment and removal of the filter plate 1.
[0007]
A support cylinder 10 is connected to the inner ring support cylinder 8, and as shown in FIG. 4, the support cylinders 10 and 10 before and after the filtration chamber 9 are supported on the frames 12 and 12 via bearings 11 and 11. is there. A drive shaft 13 is inserted into the support cylinder 10, and a drive pulley 14 fitted to one end of the drive shaft 13 is linked to the drive machine 15. In addition, a supply path 16 for the stock solution is provided inside the drive shaft 13, and a plurality of supply ports 17 that communicate with the filtration chamber 9 are opened on the peripheral surface of the drive shaft 13. A stock solution supply chamber 18 surrounded by the inner ring support cylinder 8 and the support cylinder 10 is formed between the filtration chamber 9 and the drive shaft 13. An undiluted solution supply pipe 20 is connected to one end of the drive shaft 13 via a universal joint 19. The supply pipe 20 is connected to a sludge tank 22 via a supply pump 21, and is stored in the sludge tank 22. A certain sludge is caused to flow into the stock solution supply chamber 18 from the plurality of supply ports 17 of the drive shaft 13, and the sludge is uniformly pressed into the filtration chamber 9 from the stock solution supply chamber 18.
[0008]
As shown in FIGS. 3 and 5, the filter chamber 9 has an impeller 23 supported on a drive shaft 13 inserted into the support cylinder 10, and the side edge of the impeller 23 is brought close to the filter plate 1. The tip is retracted backward in the rotational direction. The impeller 23 is rotated in the filtration chamber 9 by operating the driving machine 15. In the embodiment of the present invention, the blades 23a of the impeller 23 are bent into four straight pieces to approximate a curved line, and the impeller 23 having six blades is arranged in the filtration chamber 9. It is set up. In this manner, if the blade 23a is bent into a straight piece and approximated to a curved line, the manufacture becomes easy. A reinforcing plate 24 is fixed to the blade 23a on the rear side in the rotational direction of the impeller 23 along the center of the blade surface. The reinforcing plate 24 is a reinforcing rib disposed on the rear surface in the rotational direction of the blade 23a so that its height gradually decreases from the boss 23b side toward the tip of the blade 23a. It is a shape that can hold down to a minimum.
[0009]
As shown in FIG. 6, a cake outlet 25 is provided on the outer peripheral ring 7 in the peripheral portion of the filtration chamber 9. A back pressure adjusting valve 26 disposed in the outlet 25 is operated by operating a cylinder 27. A back pressure is applied to the filtration chamber 9. Reference numeral 28 denotes a cake chute provided at the outlet 25, reference numeral 29 denotes a filtrate receiving trough, reference numeral 30 denotes a cleaning pipe of the filter plate 1, and reference numeral 31 denotes a cover for preventing scattering of cleaning water and the like.
[0010]
The apparatus according to the present invention is configured as described above, and the opening of the wedge wire screen 4 of the filter plate 1 is set in the range of 100 μm to 200 μm, and the impeller 23 is set at 0.1 to 1.0 rpm. When sludge is supplied from the supply path 16 of the drive shaft 13 to the central portion of the filtration chamber 9 with a press-fitting pressure of 0.1 to 0.7 Kg / cm 2 while rotating at a low speed, the sludge pushing pressure and the impeller 23 are rotated. Under pressure, it is conveyed under pressure toward the outer periphery, and moisture is separated by the wedge wire screens 4 of the left and right filter plates 1. In the vicinity of the axial center immediately after the press-fitting, sludge is concentrated mainly by the press-fitting pressure, and the impeller 23 presses the sludge with a force that overcomes the sliding frictional resistance force between the concentrated sludge and the filter plate 1, and the sludge is press-fitted. A shearing action is applied to the cake that is curved and moved by the pressure and the rotational action force of the blades 23a. The dehydrated cake can be taken out while applying back pressure by the back pressure adjusting valve 26 of the outlet 25, and the side surface of the blade 23a of the impeller 23 rotates close to the inner surface of the filter plate 1, so that the filter plate 1 Can be continuously operated without clogging. The results of the dehydration test with the sewage mixed raw sludge agglomerated with polymer (solids concentration 1.59% W / V) were as good as 78.7% cake moisture content and 98.1% SS recovery rate. . That is, if the opening of the wedge wire screen 4 is set in the range of 100 μm to 200 μm based on the pressure of the stock solution and the rotational speed of the impeller, a cake having a low water content and a filtrate having a low solid content can be obtained. Is.
[0011]
【The invention's effect】
As is apparent from the above description, the filter medium of the disk filter according to the present invention is configured as described above, and the filter plate is a metal disk in which the wedge wire screen and the annular support frame having radial ribs are joined and integrated. Since it is used as a filter medium, the strength is increased, and there is no damage against high pressure, and the filter plate can be easily attached and detached. The wedge wire screen is composed of wedge wires arranged in parallel horizontally and support rods arranged in parallel in the vertical direction to fix the wedge wires. Since the solid matter is washed away with the filtrate flowing down along the slits of the support rod on the back side, there is no accumulation of filtrate and solid matter in the slit eyes, and the frequency of washing the filter medium is also reduced.
[Brief description of the drawings]
FIG. 1 is a front view of a wedge wire screen.
FIG. 2 is a rear view of a filter plate in which a wedge wire screen is fitted in an annular support frame.
FIG. 3 is a longitudinal sectional side view of a main part in which a filtration chamber according to the present invention is held on a drive shaft.
FIG. 4 is a vertical side view of a disk filter using the filter medium according to the present invention.
FIG. 5 is a front view of an impeller disposed in a disk filter.
FIG. 6 is a longitudinal front view of a disk filter using a filter medium according to the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Filter plate 2 Wedge wire 3 Support rod 4 Wedge wire screen 5 Radial rib 6 Ring support frame 7 Outer ring 9 Filtration chamber 23 Impeller

Claims (3)

2枚の円盤状のろ過板(1、1)と外周環(7)と一対の内環支持筒(8、8)とでろ過室(9)を形成し、前記内環支持筒(8)には支持筒(10)を連結し、該支持筒(10)に駆動軸(13)を内挿し、前記駆動軸(13)の内部に原液の供給路(16)を設け、前記駆動軸(13)の周面に複数の供給口(17…)を開口して、ろ過室(9)に連通させると共に、ろ過室(9)に回転自在な羽根車(23)を配設し、前記ろ過室(9)に原液を圧入供給するろ過機において、上記ろ過板(1)がウエッジワイヤースクリーン(4)と放射状リブ(5)を有する円環支持枠(6)を接合一体化した金属円盤ろ材からなることを特徴とする円盤ろ過機のろ材。A filter chamber (9) is formed by two disk-shaped filter plates (1, 1), an outer ring (7), and a pair of inner ring support cylinders (8, 8), and the inner ring support cylinder (8). Is connected to a support cylinder (10), a drive shaft (13) is inserted into the support cylinder (10), a stock solution supply path (16) is provided inside the drive shaft (13), and the drive shaft ( 13) A plurality of supply ports (17...) Are opened on the peripheral surface to communicate with the filtration chamber (9), and a rotatable impeller (23) is disposed in the filtration chamber (9). in the filtration machine for press-fitting supplying stock to the chamber (9), the filter plates (1) are wedge wire screen (4) and the metal disc filter medium was integrally bonded to the annular support frame having radial ribs (5) (6) A filter medium for a disk filter characterized by comprising: 上記ウエッジワイヤースクリーン(4)は水平状に並列したウエッジワイヤー(2)とこのウエッジワイヤー(2)を固定するための垂直方向に並列したサポートロッド(3)からなることを特徴とする請求項1記載の円盤ろ過機のろ材。  The wedge wire screen (4) comprises a wedge wire (2) arranged in parallel horizontally and a support rod (3) arranged in parallel in a vertical direction for fixing the wedge wire (2). The filter medium of the described disk filter. 上記ウエッジワイヤースクリーン(4)の目開きが100μmから200μmの範囲にあることを特徴とする請求項1または2記載の円盤ろ過機のろ材。  The filter medium of the disk filter according to claim 1 or 2, wherein the opening of the wedge wire screen (4) is in the range of 100 µm to 200 µm.
JP25265299A 1999-09-07 1999-09-07 Disc filter filter media Expired - Fee Related JP3781253B2 (en)

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