WO1983002607A1 - Procede empechant la formation d'incrustations - Google Patents
Procede empechant la formation d'incrustations Download PDFInfo
- Publication number
- WO1983002607A1 WO1983002607A1 PCT/US1982/000121 US8200121W WO8302607A1 WO 1983002607 A1 WO1983002607 A1 WO 1983002607A1 US 8200121 W US8200121 W US 8200121W WO 8302607 A1 WO8302607 A1 WO 8302607A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- copolymer
- aqueous system
- molecular weight
- acid
- metal surfaces
- 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
- C02F5/12—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 nitrogen
Definitions
- the present invention relates to the treatment of aqueous systems, and, more particularly, to inhibiting or preventing the deposition of scale onto metal surfaces in contact with the aqueous systems.
- Typical apparatus in which the metal parts are fouled by scale deposition include evaporators, single and multi-pass cooling towers and associated equipment and the like. As the aqueous system is passed through or over the apparatus a portion of the aqueous system evaporates causing a concentration of the dissolved salts either naturally or synthetically contained in the system. These dissolved materials approach and reach a concentration at which they deposit out of the system (in certain instances they have solubility- in inverse relation to temperature) and form scale on the metal surfaces. This is especially true when the aqueous system is formed from nearby natural resources which contain various amounts of dissolved solids such as of calcium, magnesium and phosphates. Such deposits typically reduce heat transfer rates, and may impede the flow of the aqueous systems.
- a method of inhibiting the formation of scale, particularly calcium phosphate and the like, depositions on metal surfaces of apparatus in contact with circulating aqueous systems is highly desired. It is especially desired to have a method which uses an agent which is stable, non-corrosive, and easily handled, which is effective at very low dosages and which is capable of inhibiting the formation of scale on metal surfaces of apparatus in contact with aqueous systems which tend to concentrate.
- the present invention is directed to a method of inhibiting sc le formation on metal surfaces which are in contact with aqueous systems by incorporating into the aqu ous system a threshold quantity of a copoly er of 2-acrylamido-2-methylpropane sulfonic acid and acrylic or methacrylic acid or water soluble salts of said copolymers.
- the present invention is directed to a method which is more effective in inhibiting and preventing scale deposition, especially deposition of calcium phosphate found in hard water, to a greater degree than is currently available.
- ⁇ & surfaces can be achieved to a very high degree by the - ⁇ inclusion of threshold quantities of a specific copolymer of 2-acrylamido-2-methylpropane sulfonic acid and acrylic or methacrylic acid.
- the subject copolymer is formed from 2-acrylamido-2-methylpropane sulfonic acid with either acrylic acid or methacrylic acid.
- the molar ratio of the two types of monomeric units in the copolymer should be from 5:1 to 1:5, and more preferably from 2:1 to 1:2.
- the copolymer should be of low molecular weight with a weight average molecular weight of from 1,000 to 10,000, preferably from 4,000 to 6,000 and most preferably of about 5,000. Although small amounts of high molecular weight copolymer can be tolerated in the system, such high molecular weight copolymers tend to behave as flocculating agents and, therefore, their presence should be avoided.
- the copolymer is formed from carboxylic acid and sulfonic acid containing monomeric units. These acid units may be in the form of the free acid or preferably at least partially neutralized to a water soluble salt i.e. salts of alkali metals, such as sodium or potassium or ammonium salt with sodium being most preferred.
- a water soluble salt i.e. salts of alkali metals, such as sodium or potassium or ammonium salt with sodium being most preferred.
- copolymers required for use in the subject invention may contain minor amounts of up to about 5 mole percent of other monomeric units which are substantially inert with respect to the subject process such as lower (C,-C 5 ) esters of acrylic or methacrylic acid, «t» acrylonitrile and the like.
- copolymers required for use in the subject *• invention are surprisingly effective in inhibiting scale formation, particularly of calcium phosphate, when present in the aqueous system in threshold amounts which will depend, to some extent, on the nature of the aqueous
- OMPI system Normally dosages of from 0.1 to 100 parts per million and more preferably from 1 to 25 parts per million provide effective inhibition.
- the copolymer may be added to the aqueous system coming in contact with the metal surfaces of an apparatus by any convenient mode, such as by first forming a concentrated solution of the copolymer with water and then feeding the concentrated solution to the a ⁇ ueous system at some convenient point in the operation. Alternately, the subject copolymer can be added directly to the aqueous system.
- the copolymer found useful in performing the subject process can be formed by conventional vinyl polymerization techniques.
- the monomers of 2-acrylamido-2-methylporpane sulfonic acid, methacrylic acid and acrylic acid (as appropriate) are each commercially available.
- the monomers are mixed in appropriate molar ratios to form the desired product and are polymerized using conventional redox or free radical initiators. Formation of low molecular weight copolymers may require the presence of chain terminators such as alcohols and the like in manners known in the art.
- the subject copolymers have been found surprisingly effective in inhibiting scale formation especially with respect to inhibiting calcium phosphate deposition onto metal surfaces.
- Calcium ions are normally present in hard water such as obtained from natural sources as, for example, seawater, lakes, rivers, etc.
- Phosphates are normally present in aqueous systems either naturally or through treatment of the water for various purposes.
- the calcium and the phosphate form a precipitate which can be generally represented as the normal phosphate C «(PO ) although it has also been proposed to be a calcium phosphate known as hydroxyapatite which has the formula Ca (PC> 4 ) OH or 3Ca 3 ( 0 4 ) • Ca(OH) .
- a copolymer of 2-acrylamido-2-methylpropane sulfonic acid and methacrylic acid (mole ratio 1:2) as its sodium salt and having a molecular weight of about 5,000 was evaluated as a calcium phosphate scale inhibitor in a dynamic test apparatus.
- the apparatus comprises a vertical glass cylinder having an eight kilowatt cylindrical stainless steel cartridge heater inside.
- the cylinder was closed with a ballcock at the top and was equipped with temperature measurement probes at the inlet and outlet ports.
- An open plastic vessel having a five liter capacity was used as the open reservoir. This reservoir had an outlet tube connected to a centrifical pump which fed (via a rotometer) into the bottom inlet port of the cylinder.
- the outlet port is connected to the reservoir to return the aqueous fluid thereto.
- the reservoir also contains a cooling coil to maintain the reservoir water at 123° F. and a water make-up actuated by a diaphragm pump.
- the apparatus was maintained at a circulation rate of one
- OMPI gallon per minute with an inlet temperature of 123° F. , an outlet temperature of 130° F. and a pH of 8.2 + 0.1 using a. Precision pH probe.
- the aqueous system which circulates through the dynamic test apparatus was a water solution containing 750 ppm potassium chloride, 374 ppm calcium sulfate hemihydrate, 136 ppm calcium chloride, 341 ppm sodium chloride, 518 ppm magnesium sulfate heptahydrate, 380 ppm calcium as calcium carbonate and 15 ppm phosphate as PO (phosphoric acid) to simulate a hard natural water source.
- Total hardness of the aqueous system (as Ca and Mg) was 591 ppm.
- a concentrate of 1,000 ppm of the copolymer was formed and an aliquot portion was taken and mixed into the reservoir to provide a 20 ppm total dosage of copolymer in the aqueous system.
- the aqueous system being tested was circulated through the apparatus for a 22 hour period.
- the amount of calcium phosphate on the metal surface of the heater was determined by dissolving the scale formed with hydrochloric acid and conducting standard colorimetric analysis for phosphate.
- As a standard a duplicate test was performed in which the aqueous system did not contain the copolymer agent. The analysis showed that 102.6 mg. of phosphate scale formed in the standard while only 43.0 mg. formed when the subject copolymer was present in the aqueous system. This shows a 58.1 % inhibition to calcium phosphate scale formation.
- Example II A test was performed in the same manner as described in Example I above except that the copolymer used therein was replaced by a copolymer of
Abstract
Priority Applications (6)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB08325799A GB2125025B (en) | 1982-01-29 | 1982-01-29 | Process for inhibiting scale |
PCT/US1982/000121 WO1983002607A1 (fr) | 1982-01-29 | 1982-01-29 | Procede empechant la formation d'incrustations |
EP19820900853 EP0099883A4 (fr) | 1982-01-29 | 1982-01-29 | Procede empechant la formation d'incrustations. |
DE19823249177 DE3249177T1 (de) | 1982-01-29 | 1982-01-29 | Verfahren zur Unterdrückung der Kesselsteinbildung |
ES519364A ES519364A0 (es) | 1982-01-29 | 1983-01-28 | Procedimiento para inhibir la formacion de cascarilla sobre superficies metalicas en contacto con sistemas acuosos. |
SE8301135A SE8301135L (sv) | 1982-01-29 | 1983-03-01 | Forfarande for inhibering av pannstensbildning |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/US1982/000121 WO1983002607A1 (fr) | 1982-01-29 | 1982-01-29 | Procede empechant la formation d'incrustations |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1983002607A1 true WO1983002607A1 (fr) | 1983-08-04 |
Family
ID=22167790
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1982/000121 WO1983002607A1 (fr) | 1982-01-29 | 1982-01-29 | Procede empechant la formation d'incrustations |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP0099883A4 (fr) |
DE (1) | DE3249177T1 (fr) |
ES (1) | ES519364A0 (fr) |
GB (1) | GB2125025B (fr) |
SE (1) | SE8301135L (fr) |
WO (1) | WO1983002607A1 (fr) |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4575425A (en) * | 1984-12-24 | 1986-03-11 | Calgon Corporation | Process for controlling calcium oxalate scale over a wide pH range |
US4640793A (en) * | 1984-02-14 | 1987-02-03 | Calgon Corporation | Synergistic scale and corrosion inhibiting admixtures containing carboxylic acid/sulfonic acid polymers |
US4711725A (en) * | 1985-06-26 | 1987-12-08 | Rohm And Haas Co. | Method of stabilizing aqueous systems |
EP0271035A2 (fr) * | 1986-12-08 | 1988-06-15 | The B.F. Goodrich Company | Traitement des milieux aqueux par des copolymères contenant de l'acide acrylamidoalcane-sulfonique |
US4836933A (en) * | 1987-01-16 | 1989-06-06 | National Starch And Chemical Corporation | Water treatment polymer |
US4885097A (en) * | 1986-12-08 | 1989-12-05 | The B. F. Goodrich Company | Stabilization of metal ions with terpolymers containing styrene sulfonic acid |
US4889637A (en) * | 1986-12-08 | 1989-12-26 | Zahid Amjad | Scale control with terpolymers containing vinyl alcohol |
US4936987A (en) * | 1983-03-07 | 1990-06-26 | Calgon Corporation | Synergistic scale and corrosion inhibiting admixtures containing carboxylic acid/sulfonic acid polymers |
US4952326A (en) * | 1986-12-08 | 1990-08-28 | The B. F. Goodrich Company | Dispersion of particulates in an aqueous medium |
US4952327A (en) * | 1986-12-08 | 1990-08-28 | The B. F. Goodrich Company | Scale control with terpolymers containing styrene sulfonic acid |
US5282976A (en) * | 1992-07-21 | 1994-02-01 | Rhone-Poulenc Inc. | Terpolymer useful as a scale inhibitor |
US5380782A (en) * | 1993-10-04 | 1995-01-10 | Rohm And Haas Company | Polymeric dispersants for ceramic materials |
EP0877002A2 (fr) * | 1997-05-09 | 1998-11-11 | Rohm And Haas Company | Agents antitartres |
US6995120B2 (en) * | 2001-10-03 | 2006-02-07 | National Starch And Chemical Investment Holding Corporation | Scale control composition for high scaling environments |
EP2130898A1 (fr) | 2008-06-04 | 2009-12-09 | Rohm and Haas Company | Polymères et leur utilisation pour l'inhibition de la formation de tartre dans des applications de lavage de vaisselle automatique |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4221381C1 (de) * | 1992-07-02 | 1994-02-10 | Stockhausen Chem Fab Gmbh | Pfropf-Copolymerisate von ungesättigten Monomeren und Zuckern, Verfahren zu ihrer Herstellung und ihre Verwendung |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3709815A (en) * | 1971-07-01 | 1973-01-09 | Calgon Corp | Boiler water treatment |
US3709816A (en) * | 1971-07-01 | 1973-01-09 | Calgon Corp | Control of alluvial and other deposits in aqueous systems |
US3806367A (en) * | 1972-06-01 | 1974-04-23 | Bitz Lab Inc | Acrylamido-sulfonic acid polymers and their use as rust and tubercle removing agents |
US3928196A (en) * | 1973-12-05 | 1975-12-23 | Calgon Corp | Inhibition of scale deposition |
-
1982
- 1982-01-29 GB GB08325799A patent/GB2125025B/en not_active Expired
- 1982-01-29 EP EP19820900853 patent/EP0099883A4/fr not_active Withdrawn
- 1982-01-29 DE DE19823249177 patent/DE3249177T1/de not_active Withdrawn
- 1982-01-29 WO PCT/US1982/000121 patent/WO1983002607A1/fr not_active Application Discontinuation
-
1983
- 1983-01-28 ES ES519364A patent/ES519364A0/es active Granted
- 1983-03-01 SE SE8301135A patent/SE8301135L/ not_active Application Discontinuation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3709815A (en) * | 1971-07-01 | 1973-01-09 | Calgon Corp | Boiler water treatment |
US3709816A (en) * | 1971-07-01 | 1973-01-09 | Calgon Corp | Control of alluvial and other deposits in aqueous systems |
US3806367A (en) * | 1972-06-01 | 1974-04-23 | Bitz Lab Inc | Acrylamido-sulfonic acid polymers and their use as rust and tubercle removing agents |
US3928196A (en) * | 1973-12-05 | 1975-12-23 | Calgon Corp | Inhibition of scale deposition |
Non-Patent Citations (1)
Title |
---|
See also references of EP0099883A4 * |
Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4936987A (en) * | 1983-03-07 | 1990-06-26 | Calgon Corporation | Synergistic scale and corrosion inhibiting admixtures containing carboxylic acid/sulfonic acid polymers |
US4640793A (en) * | 1984-02-14 | 1987-02-03 | Calgon Corporation | Synergistic scale and corrosion inhibiting admixtures containing carboxylic acid/sulfonic acid polymers |
US4575425A (en) * | 1984-12-24 | 1986-03-11 | Calgon Corporation | Process for controlling calcium oxalate scale over a wide pH range |
US4711725A (en) * | 1985-06-26 | 1987-12-08 | Rohm And Haas Co. | Method of stabilizing aqueous systems |
US4952327A (en) * | 1986-12-08 | 1990-08-28 | The B. F. Goodrich Company | Scale control with terpolymers containing styrene sulfonic acid |
EP0271035A2 (fr) * | 1986-12-08 | 1988-06-15 | The B.F. Goodrich Company | Traitement des milieux aqueux par des copolymères contenant de l'acide acrylamidoalcane-sulfonique |
US4885097A (en) * | 1986-12-08 | 1989-12-05 | The B. F. Goodrich Company | Stabilization of metal ions with terpolymers containing styrene sulfonic acid |
US4889637A (en) * | 1986-12-08 | 1989-12-26 | Zahid Amjad | Scale control with terpolymers containing vinyl alcohol |
EP0271035A3 (en) * | 1986-12-08 | 1990-01-10 | The B.F. Goodrich Company | Treatment of aqueous medium with copolymers containing acrylamidoalkane sulfonic acid |
US4952326A (en) * | 1986-12-08 | 1990-08-28 | The B. F. Goodrich Company | Dispersion of particulates in an aqueous medium |
US4836933A (en) * | 1987-01-16 | 1989-06-06 | National Starch And Chemical Corporation | Water treatment polymer |
US5282976A (en) * | 1992-07-21 | 1994-02-01 | Rhone-Poulenc Inc. | Terpolymer useful as a scale inhibitor |
US5380782A (en) * | 1993-10-04 | 1995-01-10 | Rohm And Haas Company | Polymeric dispersants for ceramic materials |
EP0877002A2 (fr) * | 1997-05-09 | 1998-11-11 | Rohm And Haas Company | Agents antitartres |
EP0877002A3 (fr) * | 1997-05-09 | 1999-03-24 | Rohm And Haas Company | Agents antitartres |
US6114294A (en) * | 1997-05-09 | 2000-09-05 | Rohm And Haas Company | Copolymeric scale inhibitors for (Poly)phosphate scale control |
US6995120B2 (en) * | 2001-10-03 | 2006-02-07 | National Starch And Chemical Investment Holding Corporation | Scale control composition for high scaling environments |
EP2130898A1 (fr) | 2008-06-04 | 2009-12-09 | Rohm and Haas Company | Polymères et leur utilisation pour l'inhibition de la formation de tartre dans des applications de lavage de vaisselle automatique |
Also Published As
Publication number | Publication date |
---|---|
GB2125025B (en) | 1985-07-03 |
SE8301135L (sv) | 1983-07-30 |
SE8301135D0 (sv) | 1983-03-01 |
EP0099883A1 (fr) | 1984-02-08 |
GB2125025A (en) | 1984-02-29 |
GB8325799D0 (en) | 1983-10-26 |
ES8406566A1 (es) | 1984-07-01 |
ES519364A0 (es) | 1984-07-01 |
DE3249177T1 (de) | 1984-09-06 |
EP0099883A4 (fr) | 1984-05-29 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US5980776A (en) | Phosphonic acid polymers | |
US3715307A (en) | Treatment of water used in heat transfer equipment | |
US4650591A (en) | Acrylic acid/2-acrylamido-2-methylpropylsulfonic acid/2-acrylamido-2-methylpropyl phosphonic acid polymers as scale and corrosion inhibitors | |
US4536292A (en) | Carboxylic/sulfonic/quaternary ammonium polymers for use as scale and corrosion inhibitors | |
US4618448A (en) | Carboxylic/sulfonic/polyalkylene oxide polymer for use as scale, corrosion, and iron oxide deposit control | |
WO1983002607A1 (fr) | Procede empechant la formation d'incrustations | |
US7087189B2 (en) | Multifunctional calcium carbonate and calcium phosphate scale inhibitor | |
EP0082657B2 (fr) | Polyampholytes et leur utilisation | |
CA1239742A (fr) | Polymere d'acide carboxylique, d'acide sulfonique et de poly(oxyde d'alcoylene), agent anti-tarte, anti-corrosion et anti-depot d'oxyde de fer | |
CA1217692A (fr) | Methode de dispersion de matieres organiques, dans les systemes aqueux, a l'aide de copolymeres d'acide acrylique de faible masse moleculaire | |
KR20030083733A (ko) | 수성 시스템에서 스케일 형성 및 침착의 억제 방법 | |
CA1176446A (fr) | Methode de prevention de la corrosion des metaux ferreux | |
US5716529A (en) | Water-treating agent and method for treating water | |
US6001264A (en) | Water-treating agent and method for treating water | |
US4530955A (en) | Water treatment composition comprising a hydrolyzed maleic anhydride copolymer and a zinc compound | |
EP0277412A1 (fr) | Inhibition de la corrosion de métaux ferreux | |
CA2202946A1 (fr) | Polymeres a base de sulfobetaine, utiles pour empecher le depot de tartre de carbonate de calcium | |
SE450954B (sv) | Forfarande for behandling av hart kokarvatten | |
US4693829A (en) | Use of carboxylic acid/sulfonic acid copolymers as aluminum ion stabilizers | |
US4680135A (en) | Carboxylic/sulfonic polymer and carboxylic/polyalkylene oxide polymer admixtures for use in iron oxide deposit control | |
JP4019331B2 (ja) | 水処理剤 | |
US4765921A (en) | Acid composition with high concentrations of active materials for the treatment of water and/or cleaning installations containing same | |
JPS6260000B2 (fr) | ||
EP0218351B1 (fr) | Copolymères d'acides méthylpropylsulfonique et phosphonique et leur utilisation comme inhibiteurs de tartre et de corrosion | |
US5180790A (en) | Water soluble complexing agent for metallic cations |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
WWE | Wipo information: entry into national phase |
Ref document number: 1982900853 Country of ref document: EP |
|
AK | Designated states |
Designated state(s): DE GB JP SE US |
|
AL | Designated countries for regional patents |
Designated state(s): AT BE CH DE FR GB LU NL SE |
|
WWP | Wipo information: published in national office |
Ref document number: 1982900853 Country of ref document: EP |
|
RET | De translation (de og part 6b) |
Ref document number: 3249177 Country of ref document: DE Date of ref document: 19840906 |
|
WWE | Wipo information: entry into national phase |
Ref document number: 3249177 Country of ref document: DE |
|
WWW | Wipo information: withdrawn in national office |
Ref document number: 1982900853 Country of ref document: EP |