JPS6291204A - Membrane separator - Google Patents
Membrane separatorInfo
- Publication number
- JPS6291204A JPS6291204A JP23039885A JP23039885A JPS6291204A JP S6291204 A JPS6291204 A JP S6291204A JP 23039885 A JP23039885 A JP 23039885A JP 23039885 A JP23039885 A JP 23039885A JP S6291204 A JPS6291204 A JP S6291204A
- Authority
- JP
- Japan
- Prior art keywords
- ejector
- filtration
- tank
- liq
- filtered liquid
- 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
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は膜分離装置の改良に関するものである。[Detailed description of the invention] [Industrial application field] The present invention relates to improvements in membrane separation devices.
濾過前液タンク(17から濾過前液を膜分離装置本体(
2)の濾過前液入口(3)にポンプ(4)により送入す
る供給管路(5)と同膜分111vi、ii本体(2)
の濾過前液出口(6)から出た濾過前液を上記の濾過前
液タンクtl)に戻す戻り管路(力と膜分離装置本体(
2)の濾過済液出口(8)から出た濾過済液を濾過済液
りンク(9)に回収する回収管路0■とを備えた形式の
膜分離装置は、第1図に示すように戻り管路(7)の途
中にバルブuI3を接続して膜分離装置本体(2)内を
通る濾過前液に加圧しのって操作圧力を高めるようにし
ていた。The pre-filtration liquid is transferred from the pre-filtration liquid tank (17) to the membrane separator main body (
The supply pipe (5) which is sent by the pump (4) to the pre-filtration liquid inlet (3) of 2) and the same membrane portion 111vi, ii main body (2)
The return pipe (power and membrane separator body (
2) A membrane separator of the type equipped with a recovery pipe 0■ for recovering the filtered liquid discharged from the filtered liquid outlet (8) into the filtered liquid link (9) is as shown in Fig. 1. A valve uI3 was connected in the middle of the return pipe (7) to increase the operating pressure by pressurizing the pre-filtration liquid passing through the membrane separator main body (2).
上記し九従来の膜分離装置はバルブQGにより単に絞っ
て操作力を高めているために動力のロスが大きかった。In the nine conventional membrane separators described above, the operating force is increased by simply throttling the valve QG, resulting in a large loss of power.
本発明はバルブα0の代シにエゼクター((17Jを接
続すると共に濾過済液タンク(9)を密閉形とし、この
密閉形濾過済液夕/り(9)内の濾過済液が満されてい
ない空間0りと上記のエゼクター(αりの減圧側口−と
を接続することによって上記の動力のロスを小さくしよ
うとするものである。In the present invention, an ejector (17J) is connected to the valve α0, and the filtered liquid tank (9) is sealed, and the filtered liquid in the sealed filtered liquid tank (9) is filled with the filtered liquid. The purpose is to reduce the power loss by connecting the ejector (the depressurizing side port) to the empty space.
第2図に示す本願の実施例は濾過前液タンク(1)から
濾過前液を膜分離装置本体(2)の濾過前液入口(3)
にポンプ(4)により送入する供給管路(5)と同膜分
離装置本体(2)の濾過前液出口(6)から出た濾過前
液を上記の濾過前液タンク(1)に戻す戻り管路(7)
と膜分離装置本体(2)の濾過済液出口(8)から出た
濾過済液を濾過済液夕/り(9)に回収する回収管路(
I(14)とを備えた膜分離装置を構成し、戻υ管路(
7)の途中にエゼクター(σ2を接続すると共に濾過済
液タンク(9)を密閉形とし、この密閉形濾過済液タン
ク(9)内の濾過済液が満されていない空間α3と上記
のエゼクター(α2の減圧側口t14)とを短絡管(1
51により直結したものである。尚、図中(LDは濾過
済液の送出用ポンプ、賭は圧力計を示す。The embodiment of the present application shown in FIG.
The pre-filtration liquid discharged from the supply pipe (5) sent by the pump (4) and the pre-filtration liquid outlet (6) of the membrane separator main body (2) is returned to the above-mentioned pre-filtration liquid tank (1). Return pipe (7)
and a recovery pipe (9) for recovering the filtered liquid discharged from the filtered liquid outlet (8) of the membrane separator main body (2) to the filtered liquid outlet (9).
I (14) constitutes a membrane separation device equipped with a return υ pipe (
7), an ejector (σ2) is connected in the middle of the filter, and the filtered liquid tank (9) is sealed, and the space α3 in the sealed filtered liquid tank (9) that is not filled with filtered liquid is connected to the above-mentioned ejector. (α2 vacuum side port t14) and the short-circuit pipe (1
It is directly connected by 51. In addition, in the figure (LD indicates a pump for sending out the filtered liquid, and the mark indicates a pressure gauge.
本発明は上記のような構成であるので膜分離装置本体(
2)内を通る濾過前液の操作圧力は、エゼクター(uz
の減圧側が密閉形濾過済液タンク(9)の空間(131
と膜分離装置本体(2)の濾過済側とを減圧することと
エゼクター(112が絞って加圧することによって高め
られるものである。つtbエゼクター(t15の減圧に
より得られる操作圧力外だけ動力を小さくすることが可
能になるものであって、バルブの代りにエゼクター(u
zを利用することは動力のロスを小さくするのに有効で
ある。Since the present invention has the above-mentioned configuration, the membrane separator main body (
2) The operating pressure of the pre-filtration liquid passing through the ejector (uz
The reduced pressure side is the space (131) of the closed filtered liquid tank (9).
This is increased by reducing the pressure between the filtered side of the membrane separator main body (2) and increasing the pressure by squeezing the ejector (112). It is possible to make the size smaller, and instead of a valve, an ejector (u
Using z is effective in reducing power loss.
本発明は上記の通りであるので所期の目的を達成するこ
とができる優れた効果を奏するものである。Since the present invention is as described above, it has an excellent effect of achieving the intended purpose.
第1図は従来例を示す系統図、第2図は本発明の実施例
を示す系統図である。
(り・・・タンク、(2)・・・本体、(3)・・・入
口、(4)・・・ポンプ、(5)・・・供給管路、(6
)・・・出口、(7)・・・戻り管路、(81・・・出
口、(9)・・・タンク、00・・・回収管路、(17
J・、、エゼクター(1α3・・・空間、■・・・減圧
側口、u3・・・短絡管、ae・・・バルブ、αη・・
・ポンプ、uト・・圧力計。
食品産業挨利用
!許出願人技術研元組合FIG. 1 is a system diagram showing a conventional example, and FIG. 2 is a system diagram showing an embodiment of the present invention. (ri...tank, (2)...main body, (3)...inlet, (4)...pump, (5)...supply pipe line, (6
)...Outlet, (7)...Return pipe line, (81...Exit, (9)...Tank, 00...Recovery pipe line, (17
J・,, Ejector (1α3... Space, ■... Decompression side port, u3... Short circuit pipe, ae... Valve, αη...
・Pump, uto...pressure gauge. Use dust in the food industry! Applicant Technical Research Association
Claims (1)
2)の濾過前液入口(3)にポンプ(4)により送入す
る供給管路(5)と同膜分離装置本体(2)の濾過前液
出口(6)から出た濾過前液を上記の濾過前液タンク(
1)に戻す戻り管路(7)と膜分離装置本体(2)の濾
過済液出口(8)から出た濾過済液を濾過済液タンク(
9)に回収する回収管路(10)とを備えた膜分離装置
に於て、 戻り管路(7)の途中もしくは濾過前液出口(6)にエ
ゼクター(12)を接続すると共に濾過済液タンク(9
)を密閉形とし、この密閉形濾過済液タンク(9)内の
濾過済液が満されていない空間(13)と上記のエゼク
ター(12)の減圧側口(14)とを接続したことを特
徴とする膜分離装置。[Claims] The pre-filtration liquid is transferred from the pre-filtration liquid tank (1) to the membrane separator main body (
The pre-filtration liquid discharged from the supply pipe (5) fed by the pump (4) to the pre-filtration liquid inlet (3) of 2) and the pre-filtration liquid outlet (6) of the membrane separator main body (2) is Pre-filtration liquid tank (
1) and the filtered liquid exiting from the filtered liquid outlet (8) of the membrane separator body (2) are transferred to the filtered liquid tank (
In a membrane separation device equipped with a recovery pipe (10) for recovering the filtered liquid, an ejector (12) is connected to the middle of the return pipe (7) or to the pre-filtration liquid outlet (6), and the filtered liquid is Tank (9
) is a closed type, and the space (13) which is not filled with filtered liquid in this closed type filtered liquid tank (9) is connected to the vacuum side port (14) of the ejector (12). Features of membrane separation equipment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23039885A JPS6291204A (en) | 1985-10-16 | 1985-10-16 | Membrane separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP23039885A JPS6291204A (en) | 1985-10-16 | 1985-10-16 | Membrane separator |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6291204A true JPS6291204A (en) | 1987-04-25 |
Family
ID=16907251
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP23039885A Pending JPS6291204A (en) | 1985-10-16 | 1985-10-16 | Membrane separator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6291204A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62136206A (en) * | 1985-12-10 | 1987-06-19 | アルバニ−・インタ−ナシヨナル・コ−ポレイシヨン | Method and apparatus for separating liquid by diaphragm |
WO1996000698A1 (en) * | 1994-06-28 | 1996-01-11 | Pure Etch Co. | Rare earth recovery process |
WO1999056860A1 (en) * | 1998-05-04 | 1999-11-11 | Hermann Dengler | Device for obtaining a desalinated solution |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS53140286A (en) * | 1977-05-12 | 1978-12-07 | Hitachi Zosen Corp | Making apparatus for fresh water |
JPS5814905A (en) * | 1981-07-17 | 1983-01-28 | Toray Ind Inc | Separation apparatus by reverse osmosis |
-
1985
- 1985-10-16 JP JP23039885A patent/JPS6291204A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS53140286A (en) * | 1977-05-12 | 1978-12-07 | Hitachi Zosen Corp | Making apparatus for fresh water |
JPS5814905A (en) * | 1981-07-17 | 1983-01-28 | Toray Ind Inc | Separation apparatus by reverse osmosis |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62136206A (en) * | 1985-12-10 | 1987-06-19 | アルバニ−・インタ−ナシヨナル・コ−ポレイシヨン | Method and apparatus for separating liquid by diaphragm |
WO1996000698A1 (en) * | 1994-06-28 | 1996-01-11 | Pure Etch Co. | Rare earth recovery process |
WO1999056860A1 (en) * | 1998-05-04 | 1999-11-11 | Hermann Dengler | Device for obtaining a desalinated solution |
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