METHOD FOR CONTROLLING PHOSPHONATES TENDING TO PRECIPITATE METAL IONS IN WATER

Abstract: There is described a method for controlling phosphonates which tend to precipitate with metal ions such as calcium and zinc in water treatment operations whereby use is made of a copolymer containing at least the following monomeric units: a) where R is hydrogen, or alkyl where R₁ is an alkyl group and where X is hydrogen, NH , a water soluble metal ion or an organic base; b) a monocarboxylic acid monomer.

Description: This invention relates to a method for controlling phosphonates which normally tend to precipitate with metal ions such as calcium and zinc in water treatment. Phosphonates are since a long time used in water treatment. Phosphonates are able to control inorganic deposits, like calciumcarbonate, calciumsulfate a.s.o. They are also in use as corrosion inhibitors. Using phosphonates as scale and corrosion inhibitors in water treatment has left some important problems. As is known from the literature a lot of the common used phosphonates form insoluble phosphonate salts with cations such as for example calcium and zinc. The invention has for an object a new and original method for controlling such phosphonates in water treatment. According to the invention, use is made of a copolymer containing at least the following monomeric units: a) wherein R is hydrogen or alkyl, R₁ is an alkyl group and X is hydrogen NH, a water soluble metal ion or an organic base; b) a monocarboxylic acid monomer. Still according to the invention, said mono­ carboxylic acid is acrylic acid or methacrylic acid. Other features and advantages of the inven­ tion will appear from the description of same given hereinafter as a non limitative example. It was discovered that when adding the new polymer according to the invention in combination with phos­ phonates which normally tend to precipitate out in high calcium containing water no precipitation of insoluble phosphonate compounds will occur. In addition the protection against corrosion will be remar­ kably improved. The new polymers contain at least the following monomers: a) where R is hydrogen or aklyl; R₁ is an alkyl group and X is hydrogen NH, a water soluble metal ion or an organic base. An example of this type of monomer is the sulfuric ester of 2-hydroxy­ ethylmethacrylate (HEMA); b) Monocarboxylic acid monomers: (examples are acrylic acid, methacrylic acid). These acids may be neutralized to the salt form with bases such as for example sodiumhydroxide, ammonia, organic bases as for example ethanolamine. A part of these carboxylic acids may be replaced by other monomer units: - dicarboxylic acids such as maleic acid or anhydride, itaconic acid ; - sulfonate containing monomers such as 2-acrylamido-2-methylpropyl­ sulfonic acid, methallylsulfonic acid, vinylsulfonic acid ...; - hydroxycontaining monomers like 2-hydroxypropylacrylate, allylalcohol ...; - esters of the forementioned monomers, for example: ethylacrylate, methylmethacrylate, the phosphate ester of hydroxy­ ethylmethacrylate; - phosphorus bearing monomers like vinylphosphonic acid, allyl­ hydroxypropylphosphonate etc.; - other copolymerisable units include acrylamide, acrylonitrile, vinylacetate, acroleine, cationic monomers. The polymers may be produced, for example, by simple radicalar polymerisation techniques in water as a solvent. As initiators, use may be made of the common chemicals such as persulfate, hydrogen peroxide, benzoylperoxide. To regulate the chain length, well known materials such as sulfur bearing compounds e.g. mercaptoacetic acid, mercaptoethanol a.s.o. can be used. Other chain transfer agents are, for example, phosphorus bearing compounds such as H₃PO₃, H₃PO₂ and organic PH bearing compounds such as, for example, dialkylphosphite. Alcohols, for instance, isopropanol can also be used. The molecular weight of the polymer may vary between about 500 to about 100,000 (about 1000 to 10.000 being preferred). The ratio of [a] to [b] monomers, as referred to above, may vary from 30:1 to 1:30 (30:1 to 1:2 being preferred). The above described polymers demonstrate their phosphonate stabilising properties in the dose range of about 0,1 to 100 ppm; 1 to 20 ppm being preferred. To control phosphonate deposits the fore­ mentioned polymers may be combined with other polymers. Examples of such polymers are: - polymonocarboxylic acid, e.g. polyacrylic acid, phosphinocarboxylic acids; - polydicarboxylic acids, e.g. polymaleic acid; - polyacrylamide - copolymers of monocarboxylic or dicarboxylic acids with other co­ polymerisable units, such as: . sulfonate containing monomers, as for example, 2-acrylamido-2-methyl-propylsulfonic acid, methallysulfonic acid, styrene sulfonic acid; . hydroxycontaining monomers, such as 2-hydroxypropylacrylate, allyl-alcohol; . esters of the forementioned carboxylic acids, such as ethylacrylate, methylmethacrylate etc.... . aldehyde containing monomers, e.g. acro­ leine; . amides, e.g. acrylamide; . phosphorusbearing monomers, such as vi­ nylphosphonate, allylhydroxypropylphosphonate, hydroxyethylmethalcry­ late phosphate. Also included in the copolymers are the copolymers bearing phosphine groups as mentioned in European Patent Application 0 150 706. - Polysulfonic acids, such as polystyrenesulfonate. This list of admixed polymers merely serves as an illustration and may in no case been interpreted as a limitation. The following examples illustrate the merits of the invention: 10 ppm of different well known phosphonates are brought into contact with 400 ppm of calcium at a temperature of about 60° C during ± 30 minutes, at pH 9, eventually together with a polymer. After this period the turbidity of the sample is measured at 450 nm. The sample is then filtered over a millipore filter of 0,22 µm and the soluble phosphonate is determined. Table 1 : Stabilisation of different phos­ phonates at pH 9; TCa: 1000 ppm CaCO₃ The same effects are observed when adding at pH 9 a supplement of zinc ions to the solution. This is demonstrated in the next table, where a supplement of 2 ppm zinc is added to the solution. The HEMA-S-acrylic acid copolymer was also tested in a pilot cooling system under an all organic programm containing 3 ppm NTMPA, 2 ppm HEDP 2 ppm phosphonobutane - 1, 2, 4-tricarboxylic acid (PBTC). The water quality of the cooling water is indicated below: pH : 8,6 TAC (ppm CaCO₃) : 500 TA (ppm CaCO₃) : 30 Cl⁻ : 260 ppm SO : 240 ppm TDS : 1500 µS cm⁻¹ TCa(ppm CaCO₃) : 500 The water temperature of the cooling water was about 50°C; the retention time of the cooling system was 3 days. When using 5 ppm HEMA-S-acrylic acid copolymer as a polymer constituent, no phosphonate loss was observed during 7 days, while corrosion was completely under control. Substituting the HEMA-S-acrylic acid co­ polymer for simple polyacrylic acid, the soluble phosphonate content dropped fast, heavy calciumphosphonate deposits resulted and under deposit corrosion took place. The difference in phosphonate solubility between the two treatments is given in figure 1. In addition to the above set forth compo­ sition use can be made of other water treating chemicals such as: - zinc, inorganic phosphorus compounds such as orthophosphate, polyphosphates, organic phosphonates which stay in solution at high calcium levels; - iron complexing agents such as citric acid, gluconic acid; - passive film forming agents such as mono or polycarboxylic long alifatic chain or cylloalifatic chain compounds such as oleic acids, C₆ - C₃₆ cycloalifatic di- and polycarboxylic acids; - copper protecting chemicals such as benzotriazole, mercaptobenzo­ thiazole, tolyltriazole; - silicates. Water to be treated according to the inven­ tion is, for instance, cooling water, boiling water, water in water scrubber units, and so on.

Claims: 1. Method for controlling phosphonates which tend to precipitate with metal ions such as calcium and zinc in water treatment operations whereby use is made of a copolymer containing at least the following monomeric units: a) where R is hydrogen, or alkyl, where R₁ is an alkyl group and where X is hydrogen, NH, a water soluble metal ion or an organic base b) a monocarboxylic acid monomer 2. Method according to claim 1, whereby the monomer referred to under a) is the sulfuric ester of 2-hydroxy­ ethylmethacrylate. 3. Method according to eitherone of claims 1 - 2, whereby said carboxylic acid is acrylic acid. 4. Method according to eitherone of claims 1 - 2, whereby said carboxylic acid is methacrylic acid. 5. Method according to eitherone of claims 1 - 4, whereby said carboxylic acid is neutralized, e.g. by an inorganic or organic base. 6. Method according to eitherone of claims 1 - 5, whereby the monomeric unit referred to under point a) of claim 1 is a mixture of sulfate containing monomers. 7. Method according to eitherone of claims 1 - 6, whereby a part of said monocarboxylic acid is replaced by one of the following monomeric units: - dicarboxylic acids; - sulfonate containing monomers; - hydroxycontaining monomers; - esters of the forementioned carboxylic acids; - phosphorus containing monomers; - copolymerisable units including acrylamide, acrylonitrile, vinylacetate, acroleine. 8. Method according to eitherone of claims 1 to 7, whereby said polymer has a molecular weight of about 500 to about 100.000. 9. Method according to claim 8, whereby said molecular weight lies between 1000 and 10.000. 10. Method according to eitherone of claims 1 - 9, whereby the molar ratio between the monomers referred to under a) en b) varies between 30:1 to 1:30. 11. Method according to claim 10, whereby said molar ratio varies between 30:1 and 1:2. 12. Method according to eitherone of claims 1 - 11, whereby said polymer is added to the water to be treated in a concentration of about 0,1 ppm to 100 ppm. 13. Method according to claim 12, whereby said polymer is added to the water to be treated in a concentration of about 1 to about 20 ppm. 14. Method according to eitherone of the claims 1 to 13, whereby the above water treatment operations apply to one of the following applications: - "cooling water treatment" - "boiling water treatment: - "sugar evaporation processes" - "desalination processes" - "water scrubber units" - "secondary oil recovery"

Inventors: THEVISSEN, PETER
Applicants: DENAC N.V.
Application year: 1986
Main classification: C02F5
IPC codes: C02F5