JPH03193122A - Filtration processing equipment - Google Patents
Filtration processing equipmentInfo
- Publication number
- JPH03193122A JPH03193122A JP1333669A JP33366989A JPH03193122A JP H03193122 A JPH03193122 A JP H03193122A JP 1333669 A JP1333669 A JP 1333669A JP 33366989 A JP33366989 A JP 33366989A JP H03193122 A JPH03193122 A JP H03193122A
- Authority
- JP
- Japan
- Prior art keywords
- membrane module
- sectional area
- opening cross
- tubular
- membrane
- 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.)
- Pending
Links
Landscapes
- Filtration Of Liquid (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は夾雑物を含有する処理水をろ過するろ過処理装
置に関する。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a filtration device for filtering treated water containing impurities.
従来の技術
夾雑物を多く含むし尿などの有機性廃液を生物処理する
とともにろ過膜を用いて分離することは従来より行われ
ている。この際のろ過処理装置として、複数の管状膜を
束状に並設してなる管状内圧型の膜モジュールを複数直
列に接続したものがある。前記有機性廃液は加圧状態で
前記膜モジュールの管状膜内を通過し、この際にろ過水
と濃縮廃液とに分離される。夾雑物を多く含んだままの
状態で処理水を膜モジュールに通過させると膜モジュー
ルの管状膜が流路閉塞する。したがって、有機性廃液は
膜モジュールを通過させる前にポリマーなどの薬液の注
入やドラムスクリーンまたは遠心分離もしくはこれらの
併用により前処理される。BACKGROUND OF THE INVENTION Conventional techniques have conventionally been used to biologically treat organic wastewater such as human waste containing a large amount of impurities and to separate it using a filtration membrane. As a filtration treatment apparatus in this case, there is one in which a plurality of tubular internal pressure type membrane modules each having a plurality of tubular membranes arranged side by side in a bundle are connected in series. The organic waste liquid passes through the tubular membrane of the membrane module under pressure, and is separated into filtered water and concentrated waste liquid at this time. If the treated water is passed through the membrane module while still containing a large amount of impurities, the tubular membrane of the membrane module will block the flow path. Therefore, the organic waste liquid is pretreated by injection of a chemical solution such as a polymer, drum screening, centrifugation, or a combination thereof before passing through the membrane module.
発明が解決しようとする課題
しかしながら、上記前処理を行っても夾雑物は完全には
除去されないため、処理水の夾雑物や余剰ポリマー、特
に繊維質は流路内を流れながらからみ合って次第に肥大
化し、これにより前記管状膜の流路閉塞をひきおこす。Problems to be Solved by the Invention However, impurities are not completely removed even with the above pretreatment, so impurities and surplus polymers, especially fibers, in the treated water become entangled and gradually enlarge as they flow through the flow path. This causes flow path blockage in the tubular membrane.
管状膜の途中箇所に流路閉塞が生じると、管状膜内は加
圧状態のため流路閉塞箇所の上流および下流部分で濃縮
がさらに進行し、前記流路閉塞を生じた管状膜内はその
全長にわたって泥状の濃縮夾雑物が密に詰まる。When a flow path blockage occurs in the middle of the tubular membrane, the inside of the tubular membrane is in a pressurized state, so concentration progresses further upstream and downstream of the flow path blockage point, and the inside of the tubular membrane where the flow path blockage has occurred is concentrated. The entire length is densely packed with muddy concentrated foreign matter.
このような状態になると膜モジュールの洗浄は非常に困
難となる。これを回避すべく細かな目のストレーナを膜
モジュールの上流に設けると、配管が複雑となるしまた
圧力損失も大となり、さらには細かな夾雑物まで取除く
ため洗浄頻度が増加して手間がかかってしまう。In such a state, it becomes extremely difficult to clean the membrane module. In order to avoid this, if a fine-mesh strainer is installed upstream of the membrane module, the piping becomes complicated and the pressure loss becomes large.Furthermore, the frequency of cleaning increases to remove even the smallest impurities, which requires more effort. It will take a while.
本発明は上記問題を解決するもので、手間をかけること
なく、膜モジュールの管状膜の流路閉塞を防止できるろ
過処理装置を提供することを目的とするものである。The present invention solves the above-mentioned problem, and aims to provide a filtration treatment device that can prevent flow path clogging of a tubular membrane of a membrane module without requiring much effort.
課題を解決するための手段
上記問題を解決するために本発明は、膜モジュールの上
流に、この膜モジュールの管状膜内径よりも小さい開口
断面積の孔部を複数有し、かつその総開口断面積が前記
膜モジュールの総開口断面積以上であるプレフィルタを
配設したものである。Means for Solving the Problems In order to solve the above problems, the present invention has a plurality of holes having an opening cross-sectional area smaller than the inner diameter of the tubular membrane of the membrane module, and a total opening cross-section of the membrane module. A pre-filter whose area is equal to or larger than the total opening cross-sectional area of the membrane module is provided.
作用
上記構成により、管状膜を流路閉塞させるような大きさ
の夾雑物は膜モジュールの手前でプレンィルタにより取
除かれ、これにより管状膜の流路閉塞は防止される。プ
レフィルタの総開口断面積は膜モジュールの総開口断面
積以上であるため、圧力損失は少ない。Effect With the above configuration, contaminants of a size that would block the flow path of the tubular membrane are removed by the prefilter before the membrane module, thereby preventing the flow path of the tubular membrane from being blocked. Since the total opening cross-sectional area of the pre-filter is greater than the total opening cross-sectional area of the membrane module, pressure loss is small.
実施例 以下、本発明の一実施例を図面に基づいて説明する。Example Hereinafter, one embodiment of the present invention will be described based on the drawings.
第2図に示すように、夾雑物を含有する処理水Xが留め
られた循環槽1にはポンプ2およびろ過処理装置3が接
続され、処理水Xはポンプ2によりろ過処理装置3に圧
送されている。例えば、ろ過処理装置3の入口部分の圧
力は4 kg/、n、出口部分の圧力は1kg/a+f
とされる。ろ過処理装置3は6個の管状ろ過ユニット4
が直列に接続されて構成されている。この管状ろ過ユニ
ット4は、第1図および第2図に示すように、筒状ケー
ス5内に長さ3.8mの管状膜6がバックアッププレー
ト7間で18本並設されてなる管状内圧型の膜モジュー
ル8と、この膜モジュール8の上流の補助ケース9内に
配設された円板状のプレフィルタ10と、4
接続用ジヨイント11とからなる。膜モジュール8にお
いては、圧力がかけられた処理水Xが管状膜6によりろ
過水と濃縮処理水とに分離され、ろ過水が図示しないろ
過排水口から送り出される。プレフィルタ10には、第
3図(a)に示すように、下流側が狭くなった円錐台形
状で下流端の狭路開口断面積が管状膜6の内径よりも小
さい(例えば約172の)孔部12が複数形成されてい
る。プレフィルタ10は孔部12の総狭路開口断面積が
膜モジュール8の管状膜6の総開口断面積と等しくされ
ている。As shown in FIG. 2, a pump 2 and a filtration device 3 are connected to a circulation tank 1 in which treated water X containing impurities is stored, and the treated water ing. For example, the pressure at the inlet of the filtration treatment device 3 is 4 kg/, n, and the pressure at the outlet is 1 kg/a+f.
It is said that The filtration processing device 3 includes six tubular filtration units 4
are connected in series. As shown in FIGS. 1 and 2, this tubular filtration unit 4 is a tubular internal pressure type in which 18 tubular membranes 6 each having a length of 3.8 m are arranged in parallel between backup plates 7 in a cylindrical case 5. It consists of a membrane module 8, a disc-shaped prefilter 10 disposed in an auxiliary case 9 upstream of the membrane module 8, and a connection joint 11. In the membrane module 8, the pressurized treated water X is separated into filtrated water and concentrated treated water by the tubular membrane 6, and the filtrated water is sent out from a filtration drain port (not shown). As shown in FIG. 3(a), the pre-filter 10 has holes in the shape of a truncated cone that are narrowed on the downstream side and whose narrow opening cross-sectional area at the downstream end is smaller than the inner diameter of the tubular membrane 6 (for example, about 172 holes). A plurality of portions 12 are formed. In the pre-filter 10, the total narrow opening cross-sectional area of the pores 12 is made equal to the total opening cross-sectional area of the tubular membrane 6 of the membrane module 8.
上記構成において、処理水Xはポンプ2によりろ過処理
装置3に供給され、膜モジュール8によりろ過水と濃縮
処理水とに分離される。この場合に、処理水Xには夾雑
物が含まれているが、各膜モジュール8の上流には、管
状膜6の内径よりも小さい開口断面積の孔部12が形成
されたプレフィルタ10が配設されているため、膜モジ
ュール8の管状膜6を流路閉塞させるおそれのある大き
さの夾雑物は予めプレフィルタ10により取除かれる。In the above configuration, the treated water X is supplied to the filtration treatment device 3 by the pump 2, and is separated into filtered water and concentrated treated water by the membrane module 8. In this case, although the treated water X contains impurities, a pre-filter 10 is provided upstream of each membrane module 8 in which a hole 12 having an opening cross-sectional area smaller than the inner diameter of the tubular membrane 6 is formed. Because of this, the prefilter 10 removes impurities that are large enough to potentially block the flow path of the tubular membrane 6 of the membrane module 8.
また、プレフィルタ10の総開口断面積は膜モジュール
8の総開口断面積と等しいため、プレフィルタ10によ
る圧力損失は少ない。なお、プレフィルタ10の洗浄は
、補助ケース9ごと管状ろ過ユニット4から取外すこと
により手間をかけることなく容易に行える。Further, since the total opening cross-sectional area of the pre-filter 10 is equal to the total opening cross-sectional area of the membrane module 8, the pressure loss due to the pre-filter 10 is small. Note that the prefilter 10 can be easily cleaned by removing the auxiliary case 9 from the tubular filtration unit 4 without much effort.
なお、プレフィルタlOの孔部12の形状は、第3図(
b)に示すように、上流側のみ先細りの形状であったり
、第3図(c)に示すように、単なる同一径形状であっ
てもよく、孔部12の開口断面積は膜モジュール8の総
開口断面積より大きくてもよい。The shape of the hole 12 of the pre-filter IO is shown in FIG.
As shown in b), the shape may be tapered only on the upstream side, or as shown in FIG. It may be larger than the total opening cross-sectional area.
さらに、プレフィルタ10として金網を用いてもよく、
三角から六角の格子状としてもよい。この場合の網目の
大きさは管状膜6の内径よりも小さいものが用いられ、
金網の総開口断面積は膜モジュール8の総開口断面積以
上とされる。Furthermore, a wire mesh may be used as the pre-filter 10,
It may also be in the form of a triangular to hexagonal lattice. In this case, the size of the mesh is smaller than the inner diameter of the tubular membrane 6,
The total opening cross-sectional area of the wire mesh is greater than the total opening cross-sectional area of the membrane module 8.
発明の効果
以上のように本発明によれば、膜モジュールの上流に、
管状膜の内径よりも小さい開口断面積の孔部が形成され
たプレフィルタを配設したので、管状膜を流路閉塞させ
るおそれのある夾雑物はプレフィルタで取除かれ、管状
膜の流路閉塞は防止される。また、プレフィルタの総開
口断面積を膜モジュールの総開口断面積以上としたので
、プレフィルタによる圧力損失は少ない。プレフィルタ
は簡単な構成であるため安価に製造でき、洗浄も手間を
かけることなく容易にできる。Effects of the Invention As described above, according to the present invention, upstream of the membrane module,
Since the pre-filter is provided with a pore with an opening cross-sectional area smaller than the inner diameter of the tubular membrane, the pre-filter removes contaminants that may clog the flow path of the tubular membrane. Occlusion is prevented. Further, since the total opening cross-sectional area of the pre-filter is set to be greater than or equal to the total opening cross-sectional area of the membrane module, pressure loss due to the pre-filter is small. Since the pre-filter has a simple configuration, it can be manufactured at low cost and can be easily cleaned without much effort.
図面は本発明の一実施例に係るろ過処理装置を示すもの
で、第1図は処理水の流れを表わす概略図、第2図は一
部切欠き要部拡大図、第3図は孔部形状を表わす断面図
である。
3・・・ろ過処理装置、6・・・管状膜、8・・・膜モ
ジュール、10・・・プレフィルタ、12・・・孔部、
X・・・処理水。The drawings show a filtration treatment apparatus according to an embodiment of the present invention, in which Fig. 1 is a schematic diagram showing the flow of treated water, Fig. 2 is an enlarged view of the main part with a partial cutout, and Fig. 3 is a diagram showing the pores. FIG. 3 is a cross-sectional view showing the shape. 3... Filtration processing device, 6... Tubular membrane, 8... Membrane module, 10... Pre-filter, 12... Hole section,
X... Treated water.
Claims (1)
れてなる管状内圧型の膜モジュール内に通過させながら
ろ過するろ過処理装置であって、前記膜モジュールの上
流に、前記管状膜の内径よりも小さい開口断面積の孔部
を複数有し、かつその総開口断面積が前記膜モジュール
の総開口断面積以上であるプレフィルタが配設されてな
るろ過処理装置。1. A filtration treatment device that filters treated water containing impurities by passing it through a tubular internal pressure type membrane module in which a plurality of tubular membranes are arranged in parallel, and the tubular membrane module is provided upstream of the membrane module. A filtration processing device comprising a pre-filter having a plurality of pores each having an opening cross-sectional area smaller than the inner diameter of a membrane, and a total opening cross-sectional area of the pre-filter having a total opening cross-sectional area greater than or equal to the total opening cross-sectional area of the membrane module.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1333669A JPH03193122A (en) | 1989-12-22 | 1989-12-22 | Filtration processing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1333669A JPH03193122A (en) | 1989-12-22 | 1989-12-22 | Filtration processing equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03193122A true JPH03193122A (en) | 1991-08-22 |
Family
ID=18268647
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1333669A Pending JPH03193122A (en) | 1989-12-22 | 1989-12-22 | Filtration processing equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03193122A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2016155098A (en) * | 2015-02-25 | 2016-09-01 | 三菱化学株式会社 | Separation membrane module |
| WO2025144798A1 (en) | 2023-12-29 | 2025-07-03 | Dupont Safety & Construction, Inc. | Filtration unit with a filtration element and a screening device |
-
1989
- 1989-12-22 JP JP1333669A patent/JPH03193122A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2016155098A (en) * | 2015-02-25 | 2016-09-01 | 三菱化学株式会社 | Separation membrane module |
| WO2025144798A1 (en) | 2023-12-29 | 2025-07-03 | Dupont Safety & Construction, Inc. | Filtration unit with a filtration element and a screening device |
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