WO2001064006A2 - Treatment of scale - Google Patents
Treatment of scale Download PDFInfo
- Publication number
- WO2001064006A2 WO2001064006A2 PCT/EP2001/001734 EP0101734W WO0164006A2 WO 2001064006 A2 WO2001064006 A2 WO 2001064006A2 EP 0101734 W EP0101734 W EP 0101734W WO 0164006 A2 WO0164006 A2 WO 0164006A2
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- component
- acid
- monomer
- antiscalent
- composition
- 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
- C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
- C02F5/08—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
- C02F5/10—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances
- C02F5/14—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances containing phosphorus
-
- 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
- C02F1/54—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using organic material
- C02F1/56—Macromolecular compounds
-
- 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
- C02F1/58—Treatment of water, waste water, or sewage by removing specified dissolved compounds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F5/00—Softening water; Preventing scale; Adding scale preventatives or scale removers to water, e.g. adding sequestering agents
- C02F5/08—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents
- C02F5/10—Treatment of water with complexing chemicals or other solubilising agents for softening, scale prevention or scale removal, e.g. adding sequestering agents using organic substances
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/22—Eliminating or preventing deposits, scale removal, scale prevention
Definitions
- the present invention relates to a novel method of treatment for the prevention, reduction or removal of scale in municipal and industrial waste water treatment facilities.
- the invention employs a new anti-scaling or de-scaling composition which is especially useful for the treatment of waste treatment plants prone to struvite scaling.
- struvite The precipitation of struvite is a problem that frequently occurs in sewage treatment plants, especially in anaerobic sludge digestion systems. Soluble magnesium combines with ammonia and phosphate, released during the aerobic digestion to form magnesium ammonium phosphate (MgNH 4 PO .6H 2 O) which is frequently referred to as struvite.
- Struvite is a hard, tenacious solid that is extremely difficult to remove from equipment surfaces and pipelines. It is generally encountered in sludge lines and downstream processes following biological phosphate removal and subsequent anaerobic digestion, although it can form wherever the solubility limit is exceeded. This can also be related to pH changes caused by sludge degassing.
- Struvite deposition is becoming an increasingly widespread problem for a great many waste water treatment plants, since it reduces throughputs, which could adversely affect subsequent sludge processing.
- the struvite can reduce the throughput so significantly that the plant operation has to be stopped and then the blocked pipework and other equipment must be cleaned.
- struvite deposits can only be removed completely by treatment with acid. This can be expensive and involve potentially dangerous handling and disposal of cleaning products (acidic solutions) which can also cause excessive wear to the equipment.
- the plant closure time during the cleaning operation can also be costly.
- Various proposals have been made in order to deal with this problem, many with some degree of success, but none of them have successfully overcome this problem completely
- aqueous solution comprising a terpolymer of acrylic acid, 2-acrylam ⁇ do-2-methylpropane sulphonic acid and specific non-ionic monomer in combination with a phosphonic acid or phosphonate
- the solution is at a pH between 2 and 9 and preferably includes hydrochloric acid
- the preference to using aqueous solutions at acidic pH is also apparent from the illustration of a scale treatment at a sewage treatment plant, where removal of scale is accompanied by effervescence
- Such acidic treatment would have the disadvantage of being expensive and involve potentially dangerous handling and disposal of cleaning products (acidic solutions) which can also cause excessive wear to the equipment
- this reference teaches that a combination of phosphonhydroxyacetic acid and acrylate copolymers merely disperse and suspends rather than actually dissolve calcium carbonate in cooling tower descaling experiments
- the use of terpolymers alone are said not to be capable of dissolving
- JP-A-08-099091 it is proposed to prevent the generation of struvite scale in piping by chemical reaction/crystallisation employing special separation equipment to recover the crystals of struvite
- struvite precipitating equipment adds an additional burden to the operation of the waste water treatment plant
- a water soluble polymer of molecular weight below 20,000 and containing anionic groups A water soluble polymer of molecular weight below 20,000 and containing anionic groups
- component (A) is formed from a monomer or monomer blend consisting of one or more ethylemcally unsaturated carboxylic acid monomer(s) and optionally an ethylemcally unsaturated water-soluble noniomc monomer
- component (A) is formed from a monomer or monomer blend consisting of one or more ethylemcally unsaturated carboxylic acid monomer(s) and optionally an ethylemcally unsaturated water-soluble noniomc monomer
- the antiscalent composition may be used for the treatment of any scale deposits in a water treatment facility
- the method is of particular relevance when the scale deposits comprise crystalline precipitate formed by the combination of phosphate, ammonia and magnesium, which may exist as magnesium ammonium phosphate (MgNH 4 PO 4 6H 2 O) which is generally referred to as struvite
- the method may be applied to any waste water treatment facility in which scale deposits are a particular problem, especially where the scale deposit is struvite
- the method is especially valuable in removing, reducing or preventing scale deposition in sewage treatment plants
- a further aspect of the invention relates to the treatment of any aqueous system containing struvite deposits
- a composition comprising,
- a water soluble polymer of molecular weight below 20,000 and containing amonic groups A water soluble polymer of molecular weight below 20,000 and containing amonic groups
- component (A) is formed from a monomer or monomer blend consisting of one or more ethylemcally unsaturated carboxylic acid monomer(s) and optionally an ethylemcally unsaturated water-soluble noniomc monomer
- the antiscalent composition employed in the present invention preferably comprises 25 to 75% by weight of the water soluble polymer (component A) and 25 to 75% by weight of the sequesterant (component B).
- the antiscaling composition comprises 30 to 70% by weight, most preferably 40 to 60%, of the water soluble polymer and between 30 and 70% by weight, most preferably 40 to 60%, of the sequesterant.
- the water soluble polymer component of the antiscalent composition is formed from a monomer or monomer blend consisting of one or more ethylenically unsaturated carboxylic acid monomer(s) and preferably not more that 50% by weight of an ethylenically unsaturated water-soluble nonionic monomer.
- the polymer is desirably formed from ethylenically unsaturated anionic monomer or anionic monomer blend in which the monomer blend comprises at least one ethylenically unsaturated carboxylic acid.
- the anionic carboxylic monomers may include acrylic acid, methacrylic acid, maleic acid, maleic anhydride, fumaric acid, itaconic acid and crotonic acid.
- the monomer blend may comprise any of the aforementioned anionic monomers and up to 50% by weight of an ethylenically unsaturated nonionic monomer, for instance acrylamide or methacrylamide.
- the polymers may exist in the free acid form or more preferably they are partially or fully neutralised.
- a particularly preferred water soluble polymer is the homopolymer of acrylic acid, hompolymer of maleic acid, hompolymer maleic anhydride or a copolymer of acrylic acid with either maleic acid or maleic anhydride.
- Especially preferred is the homopolymer of acrylic acid (or salt) or a copolymer of acrylic acid (or salt) with either maleic acid (or salt or anhydride) or itaconic acid (or salt or anhydride).
- the water soluble polymer is polymerised to a relatively low molecular weight.
- low molecular weight we mean that the polymer will have a molecular weight as determined by GPC of below 20,000.
- the molecular weight of the polymer may desirably be in the range 1 ,500 to 10,000, preferably 2,000 to 5,000
- the aqueous monomer solution should be between 20 and 40% concentration, preferably around 30 to 35%
- the monomer solution may also include a chain transfer agent, for instance sodium hypophosphite, 2-mercaptoethanol or isopropanol If sodium hypophosphite is used as the chain transfer agent, the amount can be as much as 2000 ppm by weight, but is preferably in the range 10 to 500 ppm by weight, particularly 10 to 50 ppm Where isopropanol is used as the chain transfer agent it is usual to use this as a part of the solvent system Thus the monomers would be mixed with an isopropanol/water mixture and then polymerised
- a suitable initiator system for instance aqueous ammonium persulphate, sodium metabisulphite or tertiary butyl hydroperoxide, optionally with other initiators is introduced
- the initiators are generally introduced into the monomer solution
- a thermal initiator system may be included
- a thermal initiator would include any suitable initiator compound that releases radicals at an elevated temperature, for instance azo compounds, such as azobisisobutyronit ⁇ le
- the temperature during polymerisation should rise to at least 70°C but preferably below 95°C
- the formed polymer may be a slightly viscous but pourable aqueous solution or could be a rigid gel
- Polymer gels may be further processed in a standard way by first comminuting the gel into smaller pieces, drying to the substantially dehydrated polymer followed by grinding to a powder Pourable solutions of the polymer do not need further processing and would normally be supplied in this form where they may be further diluted on application
- the polymers are produced as beads by suspension polymerisation or as a water-in-oil emulsion cr dispersion by water-in-oil emulsion polymerisation for example according to a process defined by EP-A-150933, EP-A-102760 or EP- A-126528.
- polymers may have a narrow polydispersity.
- polymers may have a polydispersity of below 1.5. They may be prepared in accordance with the teachings of EP-A-127388, EP-A-129329 and EP-A-185458.
- the antiscalent composition comprises as component B a sequesterant compound containing at least one phosphonate group and salts thereof.
- the invention embraces any phosphonate sequesterant compound that in combination with the water soluble anionic polymer of component A produces a beneficial effect in the removal, reduction and prevention of scale deposits, especially struvite.
- the phosphonate sequesterant comprises at least two phosphonate groups which at least one nitrogen atom, Desirably the phosphonate sequesterant can be desirably a compound of the formula I
- M is hydrogen, alkali metal or ammonium and R is selected from the group consisting of -H, -CH 2 CH 2 N(CH 2 PO 3 M 2 ) 2, -N(CH 2 PO 3 M 2 )CH 2 CH 2 N(CH 2 PO 3 M 2 ) 2 and -(CH 2 ) 6 N(CH 2 PO 3 M 2 ) 2 .
- R is selected from the group consisting of -H, -CH 2 CH 2 N(CH 2 PO 3 M 2 ) 2, -N(CH 2 PO 3 M 2 )CH 2 CH 2 N(CH 2 PO 3 M 2 ) 2 and -(CH 2 ) 6 N(CH 2 PO 3 M 2 ) 2 .
- a particularly preferred sequesterant is the compound of formula II,
- M ⁇ , 2 2 - N - CH 2 ⁇ P0 3 M 2 known as diethylenetnamine penta (methylene phosphomc acid) and including the corresponding alkali metal or ammonium salts, most preferred are the sodium salts
- the phosphonate sequesterant may be any one of a number of commercially available sequesterant products, for example Dequest R TM 2066 which is a post acidified sodium salt of diethylenetnamine penta (methylene phosphomc acid) available from Solutia
- the antiscalent composition is generally prepared by mixing an aqueous solution of the anionic water soluble polymer component with an aqueous solution of the phosphonate sequesterant Generally the composition does not require any added mineral acid, such as hydrochloric acid or sulphuric acid In fact effective antiscaling and scale prevention are achieved by a composition which contains substantially no substantial amount of any other ingredients Thus preferably the antiscalent composition consisting essentially of component (A) and component (B)
- the antiscalent composition may be applied at any point in the waste water treatment process Desirably though it may be applied more effectively shortly before where the scale or struvite deposits have formed or are prone to form Struvite tends to form in pipes where waste waters stand between intermittent flows, or in areas of turbulent flow, for instance where a pressure change or cavitation occurs
- struvite deposition occurs most frequently in pipes, pipe elbows, valves, centrifuge weir overflows, pumps etc , it may be desirable to dose at or prior to these points
- the antiscalent composition may be added in any effective amount, for instance up to 100 ppm This dose is based on active sequestera ⁇ t/polymer content per volume of waste water/substrate to be treated i.e. mg active antiscalent composition per litre of waste water. Generally though effective scale prevention/reduction may be achieved with much smaller doses, for instance 5 or 10 ppm, but may be as low as 2 or 3 ppm.
- scale/struvite can be effectively reduced or removed by an initial treatment of the antiscalent composition, for instance in the range 10 to 60 ppm, more preferably in the range 20 to 40 ppm. Following this initial treatment we have surprisingly found that sustained scale/struvite prevention can be achieved using reduced doses of the antiscalent composition, for instance between 5 or 10ppm lower than the initial dose.
- the sewage treatment plant has a primary treatment stage which comprises a moving bed biofilm process biological reactors. In addition there is a pre-screening and pumping of the primary sewage.
- the secondary treatment stage includes intermediate contact/settlement and fine bubble aeration (conventional activated sludge).
- the primary sewage sludge and secondary activated sludge are anaerobically digested prior to centrifuge dewate ng and pelletising in a drier. The plant was experiencing struvite build-up in the centrate discharge lines.
- An antiscalent composition comprising A) 48% w/w sodium salt of a sodium polyacrylate of molecular weight 4,500 to 5,000 (measured by GPC) aqueous solution as a 40 weight % active polymer content and B) 52% sodium salt of diethylenetriaminpenta (methylenephosphonic acid) provided as a 45 to 49% post acidified aqueous solution.
- the antiscalent composition is dosed at 30 mg/l (based on active antiscalent per litre of substrate) after the common sludge feed approximately 100 metres before the centrifuge
- the treatment showed that struvite deposition was reduced from about 330 mg/m 2 to 160 mg/m 3 sludge flow
- a plant trial was carried out at a waste water treatment plant which had been suffering from struvite deposition
- the preliminary and primary treatment of the wastewater is treated in non-nitrifying activated sludge plant then in nitrifying trickling filters
- the secondary activated sludge is co-settled in primary tanks then anaerobically digested and dewatered in a centrifuge
- a Bardenpho plant is installed to treat part of the flow with an anaerobic/aerobic sequence to facilitate phosphorus uptake and an anoxic/aerobic recycle sequence to remove ammomcal nitrogen and prevent struvite precipitation
- an anoxic/aerobic recycle sequence to remove ammomcal nitrogen and prevent struvite precipitation
- the plant does experience struvite precipitation in the digested sludge pipelines
- Example 1 The antiscalent composition of Example 1 is dosed to the digested sludge pipelines at a dose of 50mg/l, with the result of preventing struvite precipitation
Abstract
Description
Claims
Priority Applications (7)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001562921A JP2003530204A (en) | 2000-02-29 | 2001-02-16 | Scale processing |
AU5464601A AU5464601A (en) | 2000-02-29 | 2001-02-16 | Treatment of scale |
KR1020027011153A KR20020075451A (en) | 2000-02-29 | 2001-02-16 | Treatment of scale |
CA002401271A CA2401271C (en) | 2000-02-29 | 2001-02-16 | Treatment of scale |
AU2001254646A AU2001254646B2 (en) | 2000-02-29 | 2001-02-16 | Treatment of scale |
EP01927673A EP1332114A2 (en) | 2000-02-29 | 2001-02-16 | Treatment of scale |
HU0301809A HUP0301809A2 (en) | 2000-02-29 | 2001-02-16 | Treatment of scale |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/515,729 | 2000-02-29 | ||
US09/515,729 US6391207B1 (en) | 2000-02-29 | 2000-02-29 | Treatment of scale |
Publications (2)
Publication Number | Publication Date |
---|---|
WO2001064006A2 true WO2001064006A2 (en) | 2001-09-07 |
WO2001064006A3 WO2001064006A3 (en) | 2003-05-08 |
Family
ID=24052504
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/EP2001/001734 WO2001064006A2 (en) | 2000-02-29 | 2001-02-16 | Treatment of scale |
Country Status (8)
Country | Link |
---|---|
US (1) | US6391207B1 (en) |
EP (1) | EP1332114A2 (en) |
JP (1) | JP2003530204A (en) |
KR (1) | KR20020075451A (en) |
AU (2) | AU2001254646B2 (en) |
CA (1) | CA2401271C (en) |
HU (1) | HUP0301809A2 (en) |
WO (1) | WO2001064006A2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CZ302805B6 (en) * | 2010-05-28 | 2011-11-16 | Vysoká Škola Chemicko-Technologická | Removal of deposits and inhibition of corrosion on heat-exchange surfaces of power plants |
CN103739091A (en) * | 2014-01-08 | 2014-04-23 | 河南工业大学 | Method for preventing anaerobic effluent struvite scaling |
Families Citing this family (21)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6589461B2 (en) * | 1999-11-18 | 2003-07-08 | Hansen, Incapacitated Austin C. | Method of making a treatment chemical cartridge |
MY129053A (en) * | 2001-06-06 | 2007-03-30 | Thermphos Trading Gmbh | Composition for inhibiting calcium salt scale |
DE10207088A1 (en) * | 2002-02-20 | 2003-08-28 | Bayer Ag | Prevention of incrustations of phosphate-containing double salts |
US6863825B2 (en) * | 2003-01-29 | 2005-03-08 | Union Oil Company Of California | Process for removing arsenic from aqueous streams |
US7182872B2 (en) * | 2003-08-01 | 2007-02-27 | Wisconsin Alumni Research Foundation | Struvite crystallization |
US7396453B1 (en) * | 2005-04-19 | 2008-07-08 | Procorp Enterprises, Llc | Hydraulically integrated solids/liquid separation system for wastewater treatment |
US7270796B2 (en) * | 2005-08-11 | 2007-09-18 | Castion Corporation | Ammonium/ammonia removal from a stream |
US20080053909A1 (en) * | 2006-09-06 | 2008-03-06 | Fassbender Alexander G | Ammonia recovery process |
US20080156726A1 (en) * | 2006-09-06 | 2008-07-03 | Fassbender Alexander G | Integrating recycle stream ammonia treatment with biological nutrient removal |
US20080053913A1 (en) * | 2006-09-06 | 2008-03-06 | Fassbender Alexander G | Nutrient recovery process |
US8066874B2 (en) | 2006-12-28 | 2011-11-29 | Molycorp Minerals, Llc | Apparatus for treating a flow of an aqueous solution containing arsenic |
US8349764B2 (en) * | 2007-10-31 | 2013-01-08 | Molycorp Minerals, Llc | Composition for treating a fluid |
US20090107925A1 (en) * | 2007-10-31 | 2009-04-30 | Chevron U.S.A. Inc. | Apparatus and process for treating an aqueous solution containing biological contaminants |
US8252087B2 (en) | 2007-10-31 | 2012-08-28 | Molycorp Minerals, Llc | Process and apparatus for treating a gas containing a contaminant |
US8153006B1 (en) | 2008-06-05 | 2012-04-10 | Procorp Enterprises, Llc | Anaerobic treatment process for ethanol production |
KR20120094896A (en) * | 2009-07-06 | 2012-08-27 | 몰리코프 미네랄스, 엘엘씨 | Ceria for use as an antimicrobial barrier and disinfectant in a wound dressing |
US8398855B1 (en) | 2009-09-30 | 2013-03-19 | Philip Bruno Pedros | BioCAST process |
US9233863B2 (en) | 2011-04-13 | 2016-01-12 | Molycorp Minerals, Llc | Rare earth removal of hydrated and hydroxyl species |
US20120318745A1 (en) * | 2011-06-17 | 2012-12-20 | Multiform Harvest Inc. | Method for inhibiting flocculation in wastewater treatment |
US10287198B1 (en) | 2012-09-19 | 2019-05-14 | Premier Magnesia, Llc | Compositions and methods for treating wastewater |
EP3113859A4 (en) | 2014-03-07 | 2017-10-04 | Secure Natural Resources LLC | Cerium (iv) oxide with exceptional arsenic removal properties |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4900451A (en) * | 1989-02-01 | 1990-02-13 | Betz Laboratories, Inc. | Method of controlling manganese deposition in open recirculating aqueous systems |
US5352365A (en) * | 1993-02-22 | 1994-10-04 | Fuller Richard L | Process for removing scale, and reducing scale formation in sewage treatment plants |
US5454954A (en) * | 1993-09-21 | 1995-10-03 | Calgon Corporation | Scale control in metal mining circuits using polyether polyamino methylene phosphonates |
US6063289A (en) * | 1998-10-01 | 2000-05-16 | Albright & Wilson Americas Inc. | Method for controlling scale using synergistic phosphonate blends |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4506062A (en) | 1982-08-09 | 1985-03-19 | Allied Colloids Limited | Inverse suspension polymerization process |
GB8309275D0 (en) | 1983-04-06 | 1983-05-11 | Allied Colloids Ltd | Dissolution of water soluble polymers in water |
DE3479223D1 (en) | 1983-05-20 | 1989-09-07 | Allied Colloids Ltd | Water soluble polymers and dispersions containing them |
GB8401206D0 (en) | 1984-01-17 | 1984-02-22 | Allied Colloids Ltd | Polymers and aqueous solutions |
GB8428984D0 (en) | 1984-11-16 | 1984-12-27 | Allied Colloids Ltd | Water soluble polymers |
US5087376A (en) * | 1990-10-15 | 1992-02-11 | Calgon Corporation | Multifunctional scale inhibitors |
US5593595A (en) * | 1995-10-06 | 1997-01-14 | Calgon Corporation | Method for controlling scale using a synergistic phosphonate combination |
US5798043A (en) * | 1997-12-01 | 1998-08-25 | Khudenko Engineering, Inc. | Control of anaerobic wastewater treatment |
-
2000
- 2000-02-29 US US09/515,729 patent/US6391207B1/en not_active Expired - Fee Related
-
2001
- 2001-02-16 AU AU2001254646A patent/AU2001254646B2/en not_active Ceased
- 2001-02-16 EP EP01927673A patent/EP1332114A2/en not_active Withdrawn
- 2001-02-16 CA CA002401271A patent/CA2401271C/en not_active Expired - Fee Related
- 2001-02-16 AU AU5464601A patent/AU5464601A/en active Pending
- 2001-02-16 HU HU0301809A patent/HUP0301809A2/en unknown
- 2001-02-16 KR KR1020027011153A patent/KR20020075451A/en not_active Application Discontinuation
- 2001-02-16 JP JP2001562921A patent/JP2003530204A/en active Pending
- 2001-02-16 WO PCT/EP2001/001734 patent/WO2001064006A2/en active Application Filing
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4900451A (en) * | 1989-02-01 | 1990-02-13 | Betz Laboratories, Inc. | Method of controlling manganese deposition in open recirculating aqueous systems |
US5352365A (en) * | 1993-02-22 | 1994-10-04 | Fuller Richard L | Process for removing scale, and reducing scale formation in sewage treatment plants |
US5454954A (en) * | 1993-09-21 | 1995-10-03 | Calgon Corporation | Scale control in metal mining circuits using polyether polyamino methylene phosphonates |
US6063289A (en) * | 1998-10-01 | 2000-05-16 | Albright & Wilson Americas Inc. | Method for controlling scale using synergistic phosphonate blends |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CZ302805B6 (en) * | 2010-05-28 | 2011-11-16 | Vysoká Škola Chemicko-Technologická | Removal of deposits and inhibition of corrosion on heat-exchange surfaces of power plants |
CN103739091A (en) * | 2014-01-08 | 2014-04-23 | 河南工业大学 | Method for preventing anaerobic effluent struvite scaling |
Also Published As
Publication number | Publication date |
---|---|
KR20020075451A (en) | 2002-10-04 |
HUP0301809A2 (en) | 2003-09-29 |
CA2401271A1 (en) | 2001-09-07 |
US6391207B1 (en) | 2002-05-21 |
AU5464601A (en) | 2001-09-12 |
EP1332114A2 (en) | 2003-08-06 |
WO2001064006A3 (en) | 2003-05-08 |
AU2001254646B2 (en) | 2006-09-21 |
JP2003530204A (en) | 2003-10-14 |
CA2401271C (en) | 2007-03-13 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU2001254646B2 (en) | Treatment of scale | |
AU2001254646A1 (en) | Treatment of scale | |
EP1346957B1 (en) | Multifonctional calcium carbonate and calcium phospate scale inhibitor | |
US3879288A (en) | Process of inhibiting scale formation on walls of structures containing an aqueous system | |
US5382367A (en) | Method of treating cooling water systems | |
US6932909B2 (en) | Method of treating mine drainage | |
CA2084327A1 (en) | Lime neutralization process for treating acidic waters | |
US5352365A (en) | Process for removing scale, and reducing scale formation in sewage treatment plants | |
EP0353817B1 (en) | Method for controlling scale deposition in aqueous systems using allyl sulfonate maleic anhydride polymers | |
US4147627A (en) | Process for scale control using mixtures of polycationic and polyanionic polymers | |
WO2005030655A9 (en) | Use of cerium salts to inhibit manganese deposition in water systems | |
CA2074535C (en) | Hydroxamic acid containing polymers used as corrosion inhibitors | |
US3493501A (en) | Method for the removal of suspended matter in waste water treatment | |
JP4761500B2 (en) | Inhibitor of calcium carbonate scale by slaked lime suspension and method of inhibiting calcium carbonate scale | |
EP0220726A2 (en) | Stabilization of iron in aqueous systems | |
GB1575173A (en) | Mixtures of polycationic and polyanionic polymers for scale control | |
US3753901A (en) | Flocculation of aqueous industrial wastes using polyquaternary ammonium chloride polymers | |
US3617542A (en) | Removal of phosphates from sewage effluent | |
EP0172154B1 (en) | Inhibition of scale formation with a maleate polymer | |
EP0236220B1 (en) | Scale inhibitor and method of inhibiting scale | |
US4043910A (en) | Removal of phosphorous from waste water | |
CA1038511A (en) | Removal of phosphorus from waste water | |
JP4141554B2 (en) | Method for preventing phosphorus from being eluted in sludge and phosphorus elution preventing agent for sludge | |
JP3901292B2 (en) | Activated sludge bulking inhibitor and wastewater treatment method | |
JP7155369B2 (en) | Method for removing calcium from wastewater containing calcium and equipment for removing calcium |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A2 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BY BZ CA CH CN CR CU CZ DE DK DM DZ EE ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NO NZ PL PT RO RU SD SE SG SI SK SL TJ TM TR TT TZ UA UG UZ VN YU ZA ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A2 Designated state(s): GH GM KE LS MW MZ SD SL SZ TZ UG ZW AM AZ BY KG KZ MD RU TJ TM AT BE CH CY DE DK ES FI FR GB GR IE IT LU MC NL PT SE TR BF BJ CF CG CI CM GA GN GW ML MR NE SN TD TG |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
WWE | Wipo information: entry into national phase |
Ref document number: 2001927673 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 1020027011153 Country of ref document: KR Ref document number: 2401271 Country of ref document: CA |
|
ENP | Entry into the national phase |
Ref country code: JP Ref document number: 2001 562921 Kind code of ref document: A Format of ref document f/p: F |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2001254646 Country of ref document: AU |
|
WWP | Wipo information: published in national office |
Ref document number: 1020027011153 Country of ref document: KR |
|
REG | Reference to national code |
Ref country code: DE Ref legal event code: 8642 |
|
WWP | Wipo information: published in national office |
Ref document number: 2001927673 Country of ref document: EP |