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
  • C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
  • C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
• • 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
  • C02F2103/42—Nature of the water, waste water, sewage or sludge to be treated from bathing facilities, e.g. swimming pools

Definitions

• the present invention relates to the removal of biguanide from aqueous sources, such as swimming pools.
• Biguanide is used as a non-chlorine swimming pool treatment to control the spread of microbes. It is generally believed that biguanide exhibits cationic properties, wherein the nitrogen atoms present in the biguanide polymer exhibit a positive charge.
• the biguanide attaches to the negatively charged membrane of the microorganism and the charged nitrogen acts to disrupt the transfer of hydrogen ions by disrupting membrane phospholipids in the cell of the microorganism.
• the microorganism uses up all of its energy in the form of ATP (Adenosine Triphosphate) and eventually dies.
• biguanide has these advantageous properties, it is generally understood that when the parts per million of biguanide falls below 50 ppm, some semi-resistant strains of microorganisms can exist.
• a hypo-chloride ejection is used which is also known as a shock treatment.
• the hypo-chloride reacts, however, with the biguanide, to form a dispersion wherein the chloride ions surround the nitrogen in the biguanide.
• the chloride ions do not displace all of the water molecules around the polymer and thus a dispersion occurs.
• Light refracts on the polymer chain of the dispersion and makes the water appear milky which is an undesirable effect, especially in swimming pools.
• one way to remove biguanide from the pool before any shock treatment with a chlorine-based compound is by oxidation which takes a number of days, for example approximately 14 days. Obviously, such a waiting period is undesirable.
• the present invention relates to a method for removing at least a portion of biguanide from an aqueous source which includes the step of introducing a composition containing a polymeric metaphosphate to an aqueous source containing biguanide in a sufficient amount to form particles containing the biguanide.
• the present invention involves the removal of biguanide or biguanide polymer from an aqueous source by bringing a composition comprising at least one polymeric metaphosphate into contact with the aqueous source.
• Biguanide is also known as imidodicarbonimidic diamide and has the formula C 2 H 7 N 5 .
• biguanide includes polymerized versions and also includes the hydrochloride (C 2 H 7 H 5 HC1), the neutral sulfate ((C 2 H 7 N 5 ) 2 -H 2 SCy2H 2 O), and the acid sulfate
• an aqueous source is any source containing water or which is water-based or aqueous-based.
• the aqueous source can be a swimming pool, a hot tub, a pond, a Jacuzzi, a cooling tower, and the like.
• the aqueous source is a swimming pool.
• the polymeric metaphosphate is preferably sodium polymetaphosphate having the formula (NaP0 3 ) x wherein x is 3 or more. More preferably x is from about 3 to about 25, more preferably from about 6 to about 20 or from about 10 to about 20. A mixture of two or more polymeric polymetaphosphates can also be used for purposes of the present invention.
• the polymeric metaphosphate is a sodium hexametaphosphate which is available from Albright and Wilson Americas, Glen Allen, Virginia.
• the product sold by Albright and Wilson further classifies the sodium hexametaphosphate with the product formulation name: metaphosphoric acid, hexasodium salt.
• the technical grade crushed SC is preferred.
• a granular material is preferred which has a mesh range of from about 60 to about 100 mesh, more preferably from about 60 to about 80 mesh.
• the polymeric metaphosphate or a composition containing the polymeric metaphosphate can be added in granular form directly into the aqueous source.
• the granular material can be simply added directly into the swimming pool and the granular material will then dissolve and/or disperse in the swimming pool with some agitation.
• the polymeric metaphosphate can be first dissolved or partially dissolved in an aqueous solution (separate from the aqueous source containing the biguanide) and then the dissolved or partially dissolved polymeric metaphosphate solution or slurry can then be added to the aqueous source containing the biguanide.
• a stabilizer can also be added to prevent any depolymerization of the polymeric metaphosphate.
• a stabilizer is poly vinyl pyrrolidone aqueous slurry and/or a hydric alcohol, such as glycerol.
• the polymeric metaphosphate(s) can be present in any concentration in the aqueous source to remove at least a portion of the biguanide present in the aqueous source.
• a sufficient amount of polymeric metaphosphate so that the polymeric metaphosphate is present in the aqueous source at a concentration of from about 1 ppm to about 30 ppm and more preferably from about 5 ppm to about 25 ppm and most preferably from about 20 ppm to about 25 ppm.
• the polymeric metaphosphate when present in the aqueous source at sufficient quantities, causes particles to form which contain biguanide and/or precipitate biguanide out of the aqueous source thus making it easy to remove the biguanide either by filtration, vacuuming, or other means of particulate removal known to those skilled in the art.
• the fiocculation that occurs precipitates out of solution and is generally in the form of particles or aggregates which are a non-sticky, non-slippery solid which allows for easy removal.
• the oxygen molecules in the polymeric metaphosphate surround the charged nitrogen atoms in the biguanide and the polymeric metaphosphate displaces most of the water molecules surrounding the biguanide. Further, it is believed that the polymeric metaphosphate allows the cross-linking of biguanide polymer chains which further enhances the expelling of water between the polymer chains of the biguanide.
• the time frame for removing the biguanide is considerably improved and is generally less than 2 days. Further, with appropriate amounts of the polymeric metaphosphate present in the aqueous source, the polymeric metaphosphate is capable of precipitating more than 99.95% of the biguanide present in an aqueous source in less than 24 hours.
• the present invention permits a user the flexibility to try biguanide instead of chlorine-based compositions such as chlorine or chlorine dioxide and if the user wishes to switch back to the use of a chlorine-based composition, the present invention allows the user to convert to the use of a chlorine-based composition in a very short time period.
• polyiminoimidocarbonyliminoimido carbonyliminohexametaylene HCl also known as polymerized biguanide, was added in sufficient amounts to have a concentration of about 50 ppm.
• the water in the aqueous circulation tank was agitated for several minutes until particles formed into a large enough size to fall out of or precipitate out of solution. The particles were white in color. The water was then tested to determine the parts per million of biguanide in the aqueous circulation tank after removal of the white particles and it was determined that at least 99.95% by weight of the biguanide was removed.

Landscapes

• Chemical & Material Sciences (AREA)
• Water Supply & Treatment (AREA)
• Life Sciences & Earth Sciences (AREA)
• Hydrology & Water Resources (AREA)
• Engineering & Computer Science (AREA)
• Environmental & Geological Engineering (AREA)
• Inorganic Chemistry (AREA)
• Organic Chemistry (AREA)
• Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
• Removal Of Specific Substances (AREA)
• Separation Of Suspended Particles By Flocculating Agents (AREA)
• Treatments Of Macromolecular Shaped Articles (AREA)
• Solid-Sorbent Or Filter-Aiding Compositions (AREA)
• Agricultural Chemicals And Associated Chemicals (AREA)

Priority Applications (8)

Applications Claiming Priority (2)

Publications (1)

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Citations (1)

• 1997
  • 1997-08-14 US US08/911,167 patent/US5824239A/en not_active Expired - Lifetime
• 1998
  • 1998-08-06 EP EP98939104A patent/EP0999994B1/en not_active Expired - Lifetime
  • 1998-08-06 BR BR9811606-1A patent/BR9811606A/pt not_active IP Right Cessation
  • 1998-08-06 NZ NZ502605A patent/NZ502605A/en unknown
  • 1998-08-06 CN CN98807976A patent/CN1270570A/zh active Pending
  • 1998-08-06 PT PT98939104T patent/PT999994E/pt unknown
  • 1998-08-06 ES ES98939104T patent/ES2169538T3/es not_active Expired - Lifetime
  • 1998-08-06 AU AU87596/98A patent/AU746355B2/en not_active Ceased
  • 1998-08-06 WO PCT/US1998/015638 patent/WO1999008966A1/en not_active Ceased
  • 1998-08-06 JP JP2000509660A patent/JP4220672B2/ja not_active Expired - Fee Related
  • 1998-08-06 AT AT98939104T patent/ATE212323T1/de not_active IP Right Cessation
  • 1998-08-06 DE DE69803576T patent/DE69803576T2/de not_active Expired - Lifetime
  • 1998-08-06 CA CA002297043A patent/CA2297043C/en not_active Expired - Fee Related
  • 1998-08-13 ZA ZA987244A patent/ZA987244B/xx unknown
  • 1998-08-14 AR ARP980104032A patent/AR008030A1/es unknown

Patent Citations (1)

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