AU2002364649A1 - Method for treating raw condensates derived from sludge drying and installation therefor - Google Patents
Method for treating raw condensates derived from sludge drying and installation thereforInfo
- Publication number
- AU2002364649A1 AU2002364649A1 AU2002364649A AU2002364649A AU2002364649A1 AU 2002364649 A1 AU2002364649 A1 AU 2002364649A1 AU 2002364649 A AU2002364649 A AU 2002364649A AU 2002364649 A AU2002364649 A AU 2002364649A AU 2002364649 A1 AU2002364649 A1 AU 2002364649A1
- Authority
- AU
- Australia
- Prior art keywords
- reverse osmosis
- separate
- permeate
- coarse
- filtered
- 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
- 238000000034 method Methods 0.000 title abstract 5
- 238000001035 drying Methods 0.000 title 1
- 238000009434 installation Methods 0.000 title 1
- 239000010802 sludge Substances 0.000 title 1
- 238000001223 reverse osmosis Methods 0.000 abstract 5
- 239000012528 membrane Substances 0.000 abstract 3
- 239000012466 permeate Substances 0.000 abstract 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract 2
- 239000012141 concentrate Substances 0.000 abstract 2
- 239000003344 environmental pollutant Substances 0.000 abstract 2
- 231100000719 pollutant Toxicity 0.000 abstract 2
- 239000000126 substance Substances 0.000 abstract 2
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract 1
- 239000001569 carbon dioxide Substances 0.000 abstract 1
- 238000001914 filtration Methods 0.000 abstract 1
- 238000011045 prefiltration Methods 0.000 abstract 1
- 239000012855 volatile organic compound Substances 0.000 abstract 1
Classifications
-
- 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
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0217—Separation of non-miscible liquids by centrifugal force
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/08—Thickening liquid suspensions by filtration
- B01D17/085—Thickening liquid suspensions by filtration with membranes
-
- 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
- B01D61/026—Reverse osmosis; Hyperfiltration comprising multiple reverse osmosis steps
-
- 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
- B01D61/04—Feed pretreatment
-
- 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
-
- 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
- C02F1/38—Treatment of water, waste water, or sewage by centrifugal separation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physics & Mathematics (AREA)
- Nanotechnology (AREA)
- Thermal Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
- Treatment Of Sludge (AREA)
- Processing Of Solid Wastes (AREA)
- Fertilizers (AREA)
Abstract
The procedure consists of storing the coarse condensates before centrifuging to separate heavy, light and intermediate phases. After storage, the intermediate phase is filtered through reverse osmosis membranes to separate a permeate and a concentrate containing chemical pollutants. The procedure consists of storing the coarse condensates before centrifuging to separate heavy, light and intermediate phases. After storage, the intermediate phase is filtered through reverse osmosis membranes to separate a permeate and a concentrate containing chemical pollutants. Prior to centrifuging the coarse condensates have a preferable temperature of 35 - 40 deg C, and before filtering by reverse osmosis they are pre-filtered through a particulate filter. Following the reverse osmosis procedure the permeate is de-gassed to remove carbon dioxide and volatile organic compounds. The plant used for the procedure has a first chamber (1A) for storing the condensate, a centrifuge (2), a second storage chamber (6), reverse osmosis membranes (8) and a particulate pre-filter (10).
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR0116227A FR2833588B1 (en) | 2001-12-14 | 2001-12-14 | PROCESS FOR PROCESSING RAW CONDENSATES FROM SLUDGE DRYING AND INSTALLATION |
| FR01/16227 | 2001-12-14 | ||
| PCT/FR2002/004336 WO2003053858A1 (en) | 2001-12-14 | 2002-12-13 | Method for treating raw condensates derived from sludge drying and installation therefor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AU2002364649A1 true AU2002364649A1 (en) | 2003-07-09 |
Family
ID=8870517
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU2002364649A Abandoned AU2002364649A1 (en) | 2001-12-14 | 2002-12-13 | Method for treating raw condensates derived from sludge drying and installation therefor |
Country Status (7)
| Country | Link |
|---|---|
| EP (1) | EP1456131B1 (en) |
| AT (1) | ATE310712T1 (en) |
| AU (1) | AU2002364649A1 (en) |
| DE (2) | DE60207608T8 (en) |
| FR (1) | FR2833588B1 (en) |
| NO (1) | NO20042520L (en) |
| WO (1) | WO2003053858A1 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101228231B (en) * | 2005-08-08 | 2012-06-06 | 第一毛织株式会社 | Flame retardant molding composition |
| CN102252331B (en) * | 2011-05-06 | 2012-12-19 | 安徽博瑞特热能设备股份有限公司 | Energy self-feed type fluidized bed sludge incineration and tail gas pollution control system |
| CN115531927A (en) * | 2022-09-19 | 2022-12-30 | 徐州中液过滤技术有限公司 | Oil dehydration impurity removal vacuum filter |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4053399A (en) * | 1975-04-30 | 1977-10-11 | Grumman Aerospace Corporation | Method and system for waste treatment |
| JPS5936587A (en) * | 1982-08-20 | 1984-02-28 | Eidai Kikai Kogyo Kk | Water producer |
| JPH05337470A (en) * | 1992-06-04 | 1993-12-21 | Konica Corp | Treatment of waste developer of non-silver salt photosensitive material |
| DE4442393C1 (en) * | 1994-11-29 | 1995-09-21 | Umweltkompatible Prozestechnik | Separation of organic matter from wort vapour condensation |
| FR2729381B1 (en) * | 1995-01-13 | 1997-04-11 | Jose Morales | PROCESS AND PLANT FOR PURIFYING AN EFFLUENT CONTAINING ORGANIC WASTE |
-
2001
- 2001-12-14 FR FR0116227A patent/FR2833588B1/en not_active Expired - Fee Related
-
2002
- 2002-12-13 DE DE60207608T patent/DE60207608T8/en not_active Expired - Fee Related
- 2002-12-13 AU AU2002364649A patent/AU2002364649A1/en not_active Abandoned
- 2002-12-13 EP EP02805378A patent/EP1456131B1/en not_active Expired - Lifetime
- 2002-12-13 DE DE02805378T patent/DE02805378T1/en active Pending
- 2002-12-13 AT AT02805378T patent/ATE310712T1/en not_active IP Right Cessation
- 2002-12-13 WO PCT/FR2002/004336 patent/WO2003053858A1/en not_active Application Discontinuation
-
2004
- 2004-06-16 NO NO20042520A patent/NO20042520L/en not_active Application Discontinuation
Also Published As
| Publication number | Publication date |
|---|---|
| NO20042520L (en) | 2004-06-16 |
| DE60207608T2 (en) | 2006-07-27 |
| ATE310712T1 (en) | 2005-12-15 |
| DE60207608D1 (en) | 2005-12-29 |
| WO2003053858A1 (en) | 2003-07-03 |
| DE02805378T1 (en) | 2005-02-10 |
| EP1456131B1 (en) | 2005-11-23 |
| DE60207608T8 (en) | 2006-12-21 |
| EP1456131A1 (en) | 2004-09-15 |
| FR2833588B1 (en) | 2004-08-27 |
| FR2833588A1 (en) | 2003-06-20 |
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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 |