WO2000037368A1 - Verwendung von öl-in-wasser-emulsionen in aeroben biologischen kläranlagen - Google Patents
Verwendung von öl-in-wasser-emulsionen in aeroben biologischen kläranlagen Download PDFInfo
- Publication number
- WO2000037368A1 WO2000037368A1 PCT/EP1999/009990 EP9909990W WO0037368A1 WO 2000037368 A1 WO2000037368 A1 WO 2000037368A1 EP 9909990 W EP9909990 W EP 9909990W WO 0037368 A1 WO0037368 A1 WO 0037368A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- oil
- acid
- saturated
- water emulsions
- fatty
- Prior art date
Links
Classifications
-
- 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
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Definitions
- the present invention relates to the use of oil-in-water emulsions for reducing the air and / or oxygen requirement of aerobic, biological sewage treatment plants.
- the present invention further relates to the use of oil-in-water emulsions to improve denitrification in aerobic, biological sewage treatment plants.
- Sewage treatment plants are used to purify municipal and / or industrial wastewater in order to remove coarse dirt particles and biodegradable substances from the wastewater.
- sewage treatment plants consist of mechanical wastewater treatment, in which the coarse dirt particles and the primary sludge are removed, and biological wastewater treatment.
- the first part of biological wastewater treatment is the so-called aeration tank.
- the activated sludge which consists of flake-forming microorganisms in the edge zone, is located in this activation tank.
- the wastewater to be cleaned is introduced into this activation tank and mixed with the activated sludge, so that a suspension of water and microorganisms is formed.
- Enzymes that are constantly formed by the microorganisms catalyze the oxidation of the organic and NH-containing wastewater constituents to CO 2 and H 2 0 or NO 2 and H 2 O. Since oxygen for the oxidation of the wastewater constituents and for the breathing of the microorganisms the suspension must be aerated.
- Aeration is generally carried out with air, with oxygen-enriched air or with pure oxygen, an oxygen concentration of 1-3 mg / l in the suspension having to be ensured.
- the aeration tank is supplied with oxygen by aeration systems which usually distribute the air and / or the oxygen in fine bubbles in the aeration tank.
- aeration systems which usually distribute the air and / or the oxygen in fine bubbles in the aeration tank.
- the object of the invention was therefore to provide substances or compositions with which the oxygen requirement and thus the energy costs in aerobic, biological sewage treatment plants can be reduced.
- the object is achieved according to the invention by using oil-in-water emulsions to reduce the air and / or oxygen requirement of aerobic biological wastewater treatment plants, the oil-in-water emulsions in the oil phase having at least one compound of the following classes of compounds or a mixture from representatives of the following connection classes included:
- saturated or unsaturated, open-chain or cyclic, normal or isomeric hydrocarbons with 8-30 carbon atoms, saturated or unsaturated fatty alcohols, saturated or unsaturated fatty acids, fatty acid monoalkyl esters, fatty acid amides or fatty acid monoalkylamides of saturated or unsaturated fatty acids, the fatty alcohols, the fatty acids and fatty acid esters of the listed compounds Have 8-30 carbon atoms,
- oil-in-water emulsions described are known from various fields. However, it was surprising to find that these emulsions have the property of reducing the oxygen demand of aerobic biological treatment plants.
- An aerobic biological wastewater treatment plant in the sense of the invention is any municipal and / or industrial wastewater treatment plant known to the person skilled in the art, in which the biodegradable wastewater constituents are eliminated from the wastewater by oxidation.
- Such treatment plants are e.g. B. in the pocketbook of urban drainage, R. Oldenburg Verlag, Kunststoff, Vienna 1990, pages 81-333, Ullmann's Encyclopedia of Industrial Chemistry, VCH-Verlag, 1995, chapter 2.1, which are hereby introduced as a reference and thus part of the disclosure are.
- These aerobic, biological sewage treatment plants preferably have an aeration tank in which the microorganisms are either suspended or immobilized, with suspended microorganisms being preferred.
- Sufficient oxygen is introduced into the aeration tank so that the oxygen concentration in the liquid surrounding the microorganisms is preferably 1-3 mg / l.
- the oxygen can be introduced into the aeration tank as atmospheric oxygen and / or as pure oxygen.
- the preparation of the emulsions to be used according to the invention in particular stable oil-in-water emulsions, is known.
- the oil component is emulsified in water by means of suitable known oil-in-water emulsifiers.
- the hydrophobic phase mainly represents the active ingredient.
- hydrophobic oil components The following are examples of hydrophobic oil components:
- saturated hydrocarbons such as octane, tetradecane, octadecane, icodecane, decene, hexadecene and technical alpha-olefins,
- Fatty alcohols such as octanol, dodecanol, tridecanol, hexadecanol, octadecanol, behenyl alcohol, Fatty acids such as capric acid, stearic acid, melissic acid, oleic acid and linolenic acid,
- Fatty acid esters such as methyl stearate, octadecyl palmitate, octyl oleic acid, glycerol mono- and trioleate, ethylene glycol dilaurate, sorbitan stearates and oleates and / or dibutyl adipate.
- - Fatty acid amides such as stearylamide, coconut fatty acid butylamide, acetic acid oleylamide and ethylene bisstearylamide.
- Terpenes such as menthol or orange terpene (companySmer Baltician HG, Hamburg).
- hydrocarbons or hydrocarbon mixtures are paraffin oil or mineral oil.
- Fats and oils on a native basis are also suitable, in particular vegetable oils and preferably rapeseed oil.
- the saturated or unsaturated fatty alcohols which can be used according to the invention as an emulsion component are, according to known methods, for. B. the oxo synthesis as oxo alcohols or after the Guerbet reaction as Guerbet alcohols.
- polyoxyalkylene compounds based on alkylene oxides and / or fatty acid glycerides of C 2 -C 8 fatty acids are used as such, which are described among others in DE-AS-1 270 542 and EP 0247 509 B1.
- terpenes are used, they are preferably used in a mixture with a saturated or unsaturated fatty alcohol.
- the proportion of the oil phase in the oil-in-water emulsion is 1-90% by weight, preferably 1-50% by weight and particularly preferably 5-30% by weight of the total emulsion.
- oil-in-water emulsions to be used according to the invention are used as such or in dilution with water or water and / or solvent-containing mixtures.
- the emulsion to be used according to the invention can be added at any location upstream or in the activation tank, an addition to the wastewater to be purified is preferred immediately before it enters the aeration tank.
- the amount added is preferably 0.1 to 1000 ppm, particularly preferably 0.5 to 200 ppm and very particularly preferably 1.0 to 50 ppm, based on the waste water to be purified.
- the emulsions used according to the invention make it possible to reduce the amount of oxygen which has to be introduced into the activation tank for the oxidation of the waste water constituents by up to 60%.
- the emulsions to be used according to the invention have little or no toxicity and can be classified in water hazard class 1. They are biodegradable.
- the test facility used as an example is shown in Figure 1 and works on the principle of upstream denitrification.
- the system consists of a reservoir 1 and a container 2, 3 for carrying out denitrification and nitrification, the container 3 being the so-called activation tank.
- the tanks 2, 3 each have a volume of 90 I.
- the storage tank 1 serves to compensate for fluctuations in the wastewater composition and is dimensioned so large that the wastewater composition remains constant over approximately 10 days.
- the test facility also has a clarification 4.
- waste water 5 l / h of waste water are pumped into the denitrification tank 2 from the storage tank 1.
- the wastewater is taken from the inlet of the Neuss-Süd sewage treatment plant in Neuss-Weckhoven, but is mechanically pre-cleaned.
- the wastewater is 70% municipal and 30% industrial in origin.
- the waste water After the waste water has passed through the denitrification 2, is reduced in the N0 2 to N 2, the waste water components to be oxidized in the aeration tank. 3
- the wastewater runs into the secondary clarification 4, in which the sewage sludge from the cleaned wastewater is separated. To maintain the biological balance, an internal recirculation flow between denitrification 2 and aeration tank 3 is maintained.
- the aeration tank 2 has a ventilation system on the bottom with which air is distributed in a fine-bubble manner.
- the amount of air introduced into the activation tank 2 is regulated so that there is an oxygen concentration of 2 mg / l in the liquid in the activation tank.
- the amount of air supplied to the activation tank 2 is measured by a rotameter.
- the oxygen concentration in the liquid is measured with an electrode from WTW.
- An oil-in-water emulsion is optionally continuously added to the feed section with a metering pump 5.
- This emulsion consisted of 14 kg of terpene, 1.0 kg of hexadecanol, 7 kg of a 75% paraffin sulfonate and 2.1 kg of water, which were melted homogeneously and then with stirring in a 60 ° C. solution of 74.5 kg of water and 1 , 4 kg of an oleyl alcohol reacted with 20 moles of ethylene oxide was poured in.
- An oil-in-water emulsion with about 2.5% solids was formed.
- the experimental plant was initially operated for several days without the addition of this emulsion until constant conditions had been established in the experimental plant. During this time u. a. continuously measured the entered air volume and the elimination performance in relation to COD (chemical oxygen demand) and nitrogen. During this time, the air intake averaged 2 l / min.
- COD chemical oxygen demand
- Another object of the present invention is the use of the designated oil-in-water emulsions to improve the denitrification of aerobic biological treatment plants, the oil-in-water emulsions, as indicated, in the oil phase at least one compound of the following classes of compounds or contain a mixture of representatives of the following classes of compounds:
- saturated or unsaturated, open-chain or cyclic, normal or isomeric hydrocarbons with 8-30 carbon atoms, saturated or unsaturated fatty alcohols, saturated or unsaturated fatty acids, fatty acid monoalkyl esters, fatty acid amides or fatty acid monoalkylamides of saturated or unsaturated fatty acids, the fatty alcohols, the fatty acids and fatty acid esters of the listed compounds Have 8-30 carbon atoms,
- the oil-in-water emulsions described are known from various fields. However, it was surprising to find that these emulsions improve denitrification in aerobic wastewater treatment plants.
- An aerobic biological wastewater treatment plant in the sense of this invention is any municipal and / or industrial wastewater treatment plant known to the person skilled in the art, in which the biodegradable wastewater constituents are eliminated from the wastewater by oxidation and which has at least one denitrification stage.
- NO 3 "is reduced to N 2.
- the denitrification stage can be arranged before or after the so-called activation tank.
- the waste water to be treated preferably first passes through the denitrification stage before it is treated in the so-called activation tank.
- the preparation of the emulsions to be used according to the invention in particular stable oil-in-water emulsions, is known.
- the oil component is emulsified in water by means of suitable known oil-in-water emulsifiers.
- the hydrophobic phase mainly represents the active ingredient.
- hydrophobic oil components The following can be mentioned as examples of hydrophobic oil components:
- saturated hydrocarbons such as octane, tetradecane, octadecane, icodecane, decene, hexadecene and technical alpha-olefins,
- - fatty alcohols such as octanol, dodecanol, tridecanol, hexadecanol, octadecanol, behenyl alcohol,
- Fatty acids such as capric acid, stearic acid, melissic acid, oleic acid and linolenic acid,
- Fatty acid esters such as methyl stearate, octadecyl palmitate, octyl oleic acid, glycerol mono- and trioleate, ethylene glycol dilaurate, sorbitan stearates and oleates and / or dibutyl adipate.
- Fatty acid amides such as stearylamide, coconut fatty acid butylamide, acetic acid oleylamide and ethylene bisstearylamide.
- Terpenes such as menthol or orange terpene (company Chemer Baltician HG, Hamburg).
- hydrocarbons or hydrocarbon mixtures are paraffin oil or mineral oil.
- Fats and oils on a native basis are also suitable, in particular vegetable oils and preferably rapeseed oil.
- the saturated or unsaturated fatty alcohols which can be used according to the invention as an emulsion component are, according to known methods, for. B. the oxo synthesis as oxo alcohols or after the Guerbet reaction as Guerbet alcohols.
- polyoxyalkylene compounds based on alkylene oxides and / or fatty acid glycerides of Ci ⁇ -Ci ⁇ fatty acids are used as such, which are described in DE-AS-1 270542 and EP 0247509 B1, among others.
- terpenes are used, they are preferably used in a mixture with a saturated or unsaturated fatty alcohol.
- the proportion of the oil phase in the oil-in-water emulsion is 1-90% by weight, preferably 1-50% by weight and particularly preferably 5-30% by weight of the total emulsion.
- oil-in-water emulsions to be used according to the invention are used as such or in dilution with water or water and / or solvent-containing mixtures.
- the emulsion to be used according to the invention can be added at any location upstream or in the aeration tank, preference being given to adding it to the waste water to be purified immediately before it enters the denitrification stage.
- the amount added is preferably 0.1 to 1000 ppm, particularly preferably 0.5 to 200 ppm and very particularly preferably 1.0 to 50 ppm, based on the waste water to be purified.
- Emulsions using have little or no toxicity and can be classified in water hazard class 1. They are biodegradable.
- the tests for the detection of the improved denitrification were carried out in a municipal biological sewage treatment plant.
- This sewage treatment plant has two lines and works on the principle of upstream denitrification.
- Each street has a denitrification, an aeration tank and a secondary clarification, through which the wastewater flows in this order.
- Both streets are constructed identically, with the lower street additionally having a metering station for the continuous addition of an oil-in-water emulsion.
- This emulsion consists of 14 kg terpene, 1.0 kg hexadecanol, 7 kg of a 75% paraffin sulfonate and 2.1 kg water, which are melted homogeneously and then with stirring in a 60 ° C warm solution from 74.5 kg water and 1 , 4 kg of an oleyl alcohol reacted with 20 moles of ethylene oxide was poured in.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Water Supply & Treatment (AREA)
- Microbiology (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Biodiversity & Conservation Biology (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Activated Sludge Processes (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Agricultural Chemicals And Associated Chemicals (AREA)
- Detergent Compositions (AREA)
Abstract
Description
Claims
Priority Applications (14)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA 2353952 CA2353952A1 (en) | 1998-12-22 | 1999-12-21 | Use of oil-in-water emulsions in aerobic biological sewage treatment plants |
BR9916465A BR9916465A (pt) | 1998-12-22 | 1999-12-21 | Emprego de emulsões óleo-em-água em estações de tratamento de esgoto aeróbico biológico |
DE59902892T DE59902892D1 (de) | 1998-12-22 | 1999-12-21 | Verwendung von öl-in-wasser-emulsionen in aeroben biologischen kläranlagen |
SK794-2001A SK7942001A3 (en) | 1998-12-22 | 1999-12-21 | Utilization of oil-in-water emulsions in aerobic biological sewage treatment plants |
HU0104809A HUP0104809A3 (en) | 1998-12-22 | 1999-12-21 | Utilization of oil-in-water emulsions in aerobic biological sewage treatment plants |
PL34842299A PL348422A1 (en) | 1998-12-22 | 1999-12-21 | Utilization of oil-in-water emulsions in aerobic biological sewage treatment plants |
AT99963552T ATE224856T1 (de) | 1998-12-22 | 1999-12-21 | Verwendung von öl-in-wasser-emulsionen in aeroben biologischen kläranlagen |
EP99963552A EP1144316B1 (de) | 1998-12-22 | 1999-12-21 | Verwendung von öl-in-wasser-emulsionen in aeroben biologischen kläranlagen |
MXPA01005945A MXPA01005945A (es) | 1998-12-22 | 1999-12-21 | Utilizacion de emulsiones de aceite en agua en plantas de tratamiento biologico, aerobico de aguas residuales.. |
AU19805/00A AU1980500A (en) | 1998-12-22 | 1999-12-21 | Utilization of oil-in-water emulsions in aerobic biological sewage treatment plants |
JP2000589448A JP2002532251A (ja) | 1998-12-22 | 1999-12-21 | 好気的生物学的廃水処理場における水中油型エマルジョンの使用 |
IL14332499A IL143324A0 (en) | 1998-12-22 | 1999-12-21 | Utilization of oil-in-water emulsions in aerobic biological sewage treatment plants |
NO20013051A NO20013051L (no) | 1998-12-22 | 2001-06-19 | Anvendelse av olje-i-vann emulsjoner i aerobisk biologisk kloakkrenseanlegg |
HK02102899.6A HK1042681A1 (zh) | 1998-12-22 | 2002-04-17 | 油包水乳劑在需氧的生物污水處理工廠中運用 |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19859054A DE19859054C2 (de) | 1998-12-22 | 1998-12-22 | Verwendung von Öl-in-Wasser-Emulsionen in aeroben biologischen Kläranlagen |
DE19859054.7 | 1998-12-22 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2000037368A1 true WO2000037368A1 (de) | 2000-06-29 |
Family
ID=7891987
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP1999/009990 WO2000037368A1 (de) | 1998-12-22 | 1999-12-21 | Verwendung von öl-in-wasser-emulsionen in aeroben biologischen kläranlagen |
Country Status (22)
Country | Link |
---|---|
EP (1) | EP1144316B1 (de) |
JP (1) | JP2002532251A (de) |
CN (1) | CN1331660A (de) |
AR (1) | AR021986A1 (de) |
AT (1) | ATE224856T1 (de) |
AU (1) | AU1980500A (de) |
BR (1) | BR9916465A (de) |
CA (1) | CA2353952A1 (de) |
CZ (1) | CZ20012279A3 (de) |
DE (2) | DE19859054C2 (de) |
ES (1) | ES2182590T3 (de) |
HK (1) | HK1042681A1 (de) |
HU (1) | HUP0104809A3 (de) |
ID (1) | ID29796A (de) |
IL (1) | IL143324A0 (de) |
MX (1) | MXPA01005945A (de) |
NO (1) | NO20013051L (de) |
PL (1) | PL348422A1 (de) |
SK (1) | SK7942001A3 (de) |
TR (1) | TR200101820T2 (de) |
WO (1) | WO2000037368A1 (de) |
ZA (1) | ZA200104401B (de) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005512770A (ja) * | 2001-12-13 | 2005-05-12 | インバイロンメンタル オペレイティング ソリューションズ インコーポレイテッド | 排水処理のプロセスおよび装置 |
EP1693446A1 (de) * | 2005-02-16 | 2006-08-23 | Realco | Zusammensetzung - Substrat für Denitrifizierende Mikroorganismen |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3298562B2 (ja) * | 1999-05-31 | 2002-07-02 | 松下電器産業株式会社 | 脱窒素促進剤およびこの脱窒素促進剤を用いた水処理方法 |
CN102285697B (zh) * | 2011-06-08 | 2013-02-06 | 南京工业大学 | 一种不饱和聚酯树脂行业废水资源化工艺 |
CN104428259B (zh) * | 2012-07-31 | 2017-03-08 | 奥瑞恩特纳米株式会社 | 微生物丛活化剂、将该微生物丛活化剂作为有效成分的抗丝状菌剂、及使用了该微生物丛活化剂的含油脂等的排水的处理方法 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3815309A1 (de) * | 1987-05-05 | 1988-11-17 | Nabil Dr Saab | Verfahren, anlage und emulgatorsubstanz zur entsorgung schadstoffhaltiger materialien |
DE4227962A1 (de) * | 1992-08-22 | 1994-03-03 | Forschungszentrum Juelich Gmbh | Verfahren und Anlage zum Sanieren von mit organischen Schadstoffen kontaminiertem Boden |
US5354480A (en) * | 1986-05-19 | 1994-10-11 | Exxon Chemical Patents Inc. | Improved method of dewatering sludge |
DE19644714A1 (de) * | 1996-10-28 | 1998-04-30 | Klaus F Dr Ing Roth | Verfahren zum Abbau von Kühlschmierstoffen |
-
1998
- 1998-12-22 DE DE19859054A patent/DE19859054C2/de not_active Expired - Fee Related
-
1999
- 1999-12-21 AU AU19805/00A patent/AU1980500A/en not_active Abandoned
- 1999-12-21 BR BR9916465A patent/BR9916465A/pt not_active IP Right Cessation
- 1999-12-21 TR TR200101820T patent/TR200101820T2/xx unknown
- 1999-12-21 MX MXPA01005945A patent/MXPA01005945A/es not_active Application Discontinuation
- 1999-12-21 WO PCT/EP1999/009990 patent/WO2000037368A1/de not_active Application Discontinuation
- 1999-12-21 AT AT99963552T patent/ATE224856T1/de not_active IP Right Cessation
- 1999-12-21 CZ CZ20012279A patent/CZ20012279A3/cs unknown
- 1999-12-21 PL PL34842299A patent/PL348422A1/xx unknown
- 1999-12-21 HU HU0104809A patent/HUP0104809A3/hu unknown
- 1999-12-21 CA CA 2353952 patent/CA2353952A1/en not_active Abandoned
- 1999-12-21 ES ES99963552T patent/ES2182590T3/es not_active Expired - Lifetime
- 1999-12-21 IL IL14332499A patent/IL143324A0/xx unknown
- 1999-12-21 ID ID20011577A patent/ID29796A/id unknown
- 1999-12-21 CN CN99815011A patent/CN1331660A/zh active Pending
- 1999-12-21 JP JP2000589448A patent/JP2002532251A/ja active Pending
- 1999-12-21 SK SK794-2001A patent/SK7942001A3/sk unknown
- 1999-12-21 DE DE59902892T patent/DE59902892D1/de not_active Expired - Fee Related
- 1999-12-21 EP EP99963552A patent/EP1144316B1/de not_active Expired - Lifetime
- 1999-12-22 AR ARP990106676 patent/AR021986A1/es not_active Application Discontinuation
-
2001
- 2001-05-29 ZA ZA200104401A patent/ZA200104401B/en unknown
- 2001-06-19 NO NO20013051A patent/NO20013051L/no not_active Application Discontinuation
-
2002
- 2002-04-17 HK HK02102899.6A patent/HK1042681A1/zh unknown
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5354480A (en) * | 1986-05-19 | 1994-10-11 | Exxon Chemical Patents Inc. | Improved method of dewatering sludge |
DE3815309A1 (de) * | 1987-05-05 | 1988-11-17 | Nabil Dr Saab | Verfahren, anlage und emulgatorsubstanz zur entsorgung schadstoffhaltiger materialien |
DE4227962A1 (de) * | 1992-08-22 | 1994-03-03 | Forschungszentrum Juelich Gmbh | Verfahren und Anlage zum Sanieren von mit organischen Schadstoffen kontaminiertem Boden |
DE19644714A1 (de) * | 1996-10-28 | 1998-04-30 | Klaus F Dr Ing Roth | Verfahren zum Abbau von Kühlschmierstoffen |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2005512770A (ja) * | 2001-12-13 | 2005-05-12 | インバイロンメンタル オペレイティング ソリューションズ インコーポレイテッド | 排水処理のプロセスおよび装置 |
EP1693446A1 (de) * | 2005-02-16 | 2006-08-23 | Realco | Zusammensetzung - Substrat für Denitrifizierende Mikroorganismen |
Also Published As
Publication number | Publication date |
---|---|
DE19859054A1 (de) | 2000-07-06 |
ZA200104401B (en) | 2002-05-29 |
EP1144316A1 (de) | 2001-10-17 |
SK7942001A3 (en) | 2001-12-03 |
PL348422A1 (en) | 2002-05-20 |
NO20013051D0 (no) | 2001-06-19 |
EP1144316B1 (de) | 2002-09-25 |
ES2182590T3 (es) | 2003-03-01 |
ID29796A (id) | 2001-10-11 |
JP2002532251A (ja) | 2002-10-02 |
CA2353952A1 (en) | 2000-06-29 |
NO20013051L (no) | 2001-06-19 |
HUP0104809A2 (hu) | 2002-04-29 |
HK1042681A1 (zh) | 2002-08-23 |
DE19859054C2 (de) | 2000-11-30 |
IL143324A0 (en) | 2002-04-21 |
CZ20012279A3 (cs) | 2002-06-12 |
CN1331660A (zh) | 2002-01-16 |
MXPA01005945A (es) | 2002-05-06 |
ATE224856T1 (de) | 2002-10-15 |
AU1980500A (en) | 2000-07-12 |
DE59902892D1 (de) | 2002-10-31 |
AR021986A1 (es) | 2002-09-04 |
BR9916465A (pt) | 2001-09-25 |
TR200101820T2 (tr) | 2002-01-21 |
HUP0104809A3 (en) | 2004-04-28 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE68904598T2 (de) | Abwasserbehandlungsverfahren. | |
DE69630236T2 (de) | Methode und vorrichtung zur biologischen behandlung von organisch belastetem abwasser | |
DE2407008B2 (de) | Verfahren zur biologischen Entfernung von organischem Kohlenstoff aus Abwasser | |
DE3032882A1 (de) | Verfahren und vorrichtung zur biologischen reinigung von abwasser | |
EP0087128A1 (de) | Verfahren und Vorrichtung zur biologischen Reinigung von phosphathaltigem Abwasser | |
DE3737309C2 (de) | ||
DD253247A5 (de) | Verfahren zur biologischen abwasserreinigung | |
WO2007068446A1 (de) | Anlage und verfahren zur erzeugung von biogas aus flüssige und feste bestandteile enthaltendem biologisch abbaubaren material, insbesondere abfallprodukten, sowie biogaserzeugungsbehälter zur verwendung bei der anlage | |
EP1531123B1 (de) | Verfahren und Anlage zur Aufbereitung von Abwässern auf Schiffen | |
EP1144316B1 (de) | Verwendung von öl-in-wasser-emulsionen in aeroben biologischen kläranlagen | |
EP1042229A1 (de) | Flotationsreaktor sowie verfahren zur flotation | |
WO1998018727A2 (de) | Verfahren und vorrichtung zur biologischen abwasserreinigung | |
DE4402442C1 (de) | Verfahren zur Verbesserung der Abwasserreinigung in Tropfkörperanlagen | |
DE2526095C3 (de) | Verfahren zum Reinigen von Abwässern, insbesondere von öl- und fetthaltigen Abwässern | |
DE2528522C3 (de) | Verfahren zum Behandeln von insbesondere öl enthaltendem Abwasser mit einem aktivierten Schlamm | |
EP0854844B1 (de) | Biologische abwasserbehandlung bei hohen schlammkonzentrationen | |
DE3150902A1 (de) | Verfahren und vorrichtung zur biologischen reinigung von abwasser | |
DE19751288A1 (de) | Antischaummittel | |
DE19938016A1 (de) | Verfahren und Vorrichtung zur biologischen Abwasserreinigung | |
DE2542167B2 (de) | Verfahren zur Flotation von in verunreinigtem Wasser dispergierten und/oder emulgieren Teilchen | |
DE102019006988A1 (de) | Verfahren und Vorrichtung zur Zuführung von Umgebungsluft in ein Gewässer oder ein mitWasser/Abwasser gefülltes Becken, z. B. in ein Belebungsbecken einer Abwasserkläranlage | |
EP0659695A1 (de) | Verfahren und Einrichtung zum Aufbereiten von Klärschlamm | |
DE3518623A1 (de) | Verfahren und vorrichtung zur reduzierung organischer inhaltstoffe in abfaellen und/oder abwaessern | |
WO2006024372A1 (de) | Verwendung von öi-in-wasser-emulsionen in anaeroben prozessen | |
DE2062310A1 (de) | Vorrichtung zur Züchtung von Kohlen Wasserstoffe verwertenden Mikroorganismen |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
WWE | Wipo information: entry into national phase |
Ref document number: 99815011.8 Country of ref document: CN |
|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AU BR CA CN CZ HU ID IL JP MX NO PL RU SG SI SK TR US ZA |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE |
|
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 1999963552 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 143324 Country of ref document: IL |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2001/04401 Country of ref document: ZA Ref document number: 200104401 Country of ref document: ZA |
|
ENP | Entry into the national phase |
Country of ref document: CA Ref document number: 2353952 Country of ref document: CA Kind code of ref document: A |
|
WWE | Wipo information: entry into national phase |
Ref document number: 7942001 Country of ref document: SK |
|
WWE | Wipo information: entry into national phase |
Ref document number: PA/a/2001/005945 Country of ref document: MX |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2001/01820 Country of ref document: TR Ref document number: PV2001-2279 Country of ref document: CZ |
|
ENP | Entry into the national phase |
Ref document number: 2000 589448 Country of ref document: JP Kind code of ref document: A |
|
WWE | Wipo information: entry into national phase |
Ref document number: 19805/00 Country of ref document: AU |
|
WWE | Wipo information: entry into national phase |
Ref document number: 09857177 Country of ref document: US |
|
WWP | Wipo information: published in national office |
Ref document number: 1999963552 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: PV2001-2279 Country of ref document: CZ |
|
WWG | Wipo information: grant in national office |
Ref document number: 1999963552 Country of ref document: EP |
|
WWR | Wipo information: refused in national office |
Ref document number: PV2001-2279 Country of ref document: CZ |