AU5472701A - Method and device for producing ultrapure water - Google Patents
Method and device for producing ultrapure waterInfo
- Publication number
- AU5472701A AU5472701A AU54727/01A AU5472701A AU5472701A AU 5472701 A AU5472701 A AU 5472701A AU 54727/01 A AU54727/01 A AU 54727/01A AU 5472701 A AU5472701 A AU 5472701A AU 5472701 A AU5472701 A AU 5472701A
- Authority
- AU
- Australia
- Prior art keywords
- bioreactor
- water
- stage
- biostatic
- membrane filter
- 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.)
- Abandoned
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/025—Reverse osmosis; Hyperfiltration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/14—Ultrafiltration; Microfiltration
- B01D61/16—Feed pretreatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/02—Membrane cleaning or sterilisation ; Membrane regeneration
- B01D65/022—Membrane sterilisation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2311/00—Details relating to membrane separation process operations and control
- B01D2311/04—Specific process operations in the feed stream; Feed pretreatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/04—Backflushing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/18—Use of gases
- B01D2321/185—Aeration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/40—Automatic control of cleaning processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
- C02F1/505—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment by oligodynamic treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/02—Non-contaminated water, e.g. for industrial water supply
- C02F2103/04—Non-contaminated water, e.g. for industrial water supply for obtaining ultra-pure water
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
Abstract
To produce an ultra-pure water, the water inflow is passed to a bioreactor (2), followed by a non-oxidizing processing stage with a biostatic action, and a final membrane filter. To produce an ultra-pure water, the water inflow is passed to a bioreactor (2), followed by a non-oxidizing processing stage with a biostatic action, and a final membrane filter. The final membrane filter (8) has a reverse osmosis action. Heavy metal compounds are added to the water in the biostatic processing stage (6), preferably copper salts and/or zinc salts, fed in together. The biological matter turnover is registered between the biostatic processing and the final stages, to set the processing actions. The water is filtered at the bioreaction stage. The water from the bioreactor is passed through an adsorption stage (5) using active carbon, before or after the biostatic processing stage. Before the water is passed into the bioreactor, it passes through a flocking and sedimentation stage. An independent claim is included for a water purification assembly with a bioreactor and especially a multiple-layer filter (2), which is cleaned by back flushing. A following dosing unit (6) adds a heavy metal biostatic agent, with a final reverse osmosis membrane filter (8). Preferred Features: A biofouling monitor (9) in front of the membrane filter measures the level of infection in the water by a germ count, to set the working of the dosing stage (6). A monitor after the bioreactor measures the assimilable organic matter (AOC) in the water, to determine the back flushing cycles of the bioreactor. An adsorber (5) is downstream of the bioreactor. A flocking and sedimentation stage (1) is in front of the bioreactor (2).
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE10015453A DE10015453C2 (en) | 2000-03-29 | 2000-03-29 | Method and device for producing ultrapure water |
DE10015453 | 2000-03-29 | ||
PCT/EP2001/003320 WO2001072645A1 (en) | 2000-03-29 | 2001-03-23 | Method and device for producing ultrapure water |
Publications (1)
Publication Number | Publication Date |
---|---|
AU5472701A true AU5472701A (en) | 2001-10-08 |
Family
ID=7636743
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
AU54727/01A Abandoned AU5472701A (en) | 2000-03-29 | 2001-03-23 | Method and device for producing ultrapure water |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP1272434B8 (en) |
AT (1) | ATE307094T1 (en) |
AU (1) | AU5472701A (en) |
DE (2) | DE10015453C2 (en) |
ES (1) | ES2250392T3 (en) |
IL (1) | IL151565A0 (en) |
WO (1) | WO2001072645A1 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB201212156D0 (en) * | 2012-07-09 | 2012-08-22 | Enviro Dev Aps | method and system for controlling fouling |
CN110342670A (en) * | 2018-04-03 | 2019-10-18 | 上海泰邑节能环保科技有限公司 | A kind of water purification equipment equipped with cleaning device |
CN110921751B (en) * | 2018-09-19 | 2021-12-17 | 宝山钢铁股份有限公司 | Treatment method and system for removing total zinc and total organic carbon in cold rolling zinc-containing wastewater |
CN115072937A (en) * | 2022-07-15 | 2022-09-20 | 山东辰广环保装备有限公司 | Pretreatment process for solving biological pollution of water treatment membrane |
CN115124198A (en) * | 2022-07-22 | 2022-09-30 | 山东辰广环保装备有限公司 | Pretreatment device for solving biological pollution of water treatment membrane |
Family Cites Families (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3490590A (en) * | 1968-01-02 | 1970-01-20 | Dorr Oliver Inc | Carbon in membrane systems |
JPS5469578A (en) * | 1977-11-15 | 1979-06-04 | Nitto Electric Ind Co Ltd | Separating method using membrane |
US5135654A (en) * | 1984-04-30 | 1992-08-04 | Kdf Fluid Treatment, Inc. | Method for treating fluids |
CH673225A5 (en) * | 1986-04-22 | 1990-02-28 | Sanosil Ag | |
JPH02293098A (en) * | 1989-05-01 | 1990-12-04 | Ebara Infilco Co Ltd | Treatment of night soil |
JPH0647118B2 (en) * | 1989-11-07 | 1994-06-22 | 荏原インフイルコ株式会社 | Organic wastewater treatment method |
DE4117234A1 (en) * | 1991-05-27 | 1992-12-03 | Winfried Prof Dr Ing Hartmeier | Compsn. for heavy metal bio:sorption - comprises an alginate gel insoluble in water |
JPH0515744A (en) * | 1991-07-10 | 1993-01-26 | Hitachi Plant Eng & Constr Co Ltd | Membrane separator |
DE69123450T2 (en) * | 1991-10-28 | 1997-06-26 | Net Co | Carrier used in a device for the treatment of organic waste water |
US5683724A (en) * | 1993-03-17 | 1997-11-04 | Ecolab Inc. | Automated process for inhibition of microbial growth in aqueous food transport or process streams |
AU2358395A (en) * | 1994-04-26 | 1995-11-16 | Seh America, Inc. | Water purification system and method |
DE19531519C2 (en) * | 1994-08-30 | 1996-11-28 | Univ Hohenheim | Microorganism capable of denitrification and its use in connection with a method for denitrification of water |
GB2303316B (en) * | 1995-07-19 | 1999-06-16 | Baker Hughes Ltd | Biofouling reduction |
DE19625346A1 (en) * | 1996-06-25 | 1998-01-02 | Joseph Dipl Ing Maier | Process for water treatment in a closed circuit with a reactor |
WO1998025858A1 (en) * | 1996-12-13 | 1998-06-18 | Alliedsignal Inc. | Closed-loop wastewater treatment system |
DE60036706T2 (en) * | 1999-02-18 | 2008-07-17 | Next-Ro, Inc., Redondo Beach | SYSTEM FOR REVERSE OSMOSIS TO PREVENT BIOLOGICAL CONTAMINATION |
-
2000
- 2000-03-29 DE DE10015453A patent/DE10015453C2/en not_active Expired - Fee Related
-
2001
- 2001-03-22 IL IL15156501A patent/IL151565A0/en not_active IP Right Cessation
- 2001-03-23 WO PCT/EP2001/003320 patent/WO2001072645A1/en active IP Right Grant
- 2001-03-23 AU AU54727/01A patent/AU5472701A/en not_active Abandoned
- 2001-03-23 EP EP01927785A patent/EP1272434B8/en not_active Expired - Lifetime
- 2001-03-23 DE DE50107747T patent/DE50107747D1/en not_active Expired - Lifetime
- 2001-03-23 ES ES01927785T patent/ES2250392T3/en not_active Expired - Lifetime
- 2001-03-23 AT AT01927785T patent/ATE307094T1/en not_active IP Right Cessation
Also Published As
Publication number | Publication date |
---|---|
ATE307094T1 (en) | 2005-11-15 |
DE10015453C2 (en) | 2002-12-19 |
DE10015453A1 (en) | 2001-10-31 |
EP1272434B8 (en) | 2005-12-28 |
WO2001072645A1 (en) | 2001-10-04 |
EP1272434A1 (en) | 2003-01-08 |
DE50107747D1 (en) | 2006-03-02 |
ES2250392T3 (en) | 2006-04-16 |
EP1272434B1 (en) | 2005-10-19 |
IL151565A0 (en) | 2003-04-10 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
MK6 | Application lapsed section 142(2)(f)/reg. 8.3(3) - pct applic. not entering national phase |