CA1211624A - Treatment of aqueous systems - Google Patents
Treatment of aqueous systemsInfo
- Publication number
- CA1211624A CA1211624A CA000425925A CA425925A CA1211624A CA 1211624 A CA1211624 A CA 1211624A CA 000425925 A CA000425925 A CA 000425925A CA 425925 A CA425925 A CA 425925A CA 1211624 A CA1211624 A CA 1211624A
- Authority
- CA
- Canada
- Prior art keywords
- phosphonate
- nitrite
- water soluble
- weight percent
- ppm
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23F—NON-MECHANICAL REMOVAL OF METALLIC MATERIAL FROM SURFACE; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL; MULTI-STEP PROCESSES FOR SURFACE TREATMENT OF METALLIC MATERIAL INVOLVING AT LEAST ONE PROCESS PROVIDED FOR IN CLASS C23 AND AT LEAST ONE PROCESS COVERED BY SUBCLASS C21D OR C22F OR CLASS C25
- C23F11/00—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent
- C23F11/08—Inhibiting corrosion of metallic material by applying inhibitors to the surface in danger of corrosion or adding them to the corrosive agent in other liquids
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Preventing Corrosion Or Incrustation Of Metals (AREA)
Abstract
A B S T R A C T
THE TREATMENT OF AQUEOUS SYSTEMS
A method of inhibiting corrosion in an aqueous system is described which comprises adding to the system at least one water soluble inorganic nitrite and at least one phosphonate which contains at least two acid groups which are carboxylic and phosphonic acid groups such that at least one acid group is a carboxylic acid group and at least one acid group is a phosphonic acid group, at least the said two acid groups being attached to carbon atoms, the concentration of phosphonate exceeding 5 ppm weight per volume and the weight ratio of nitrite to phosphonate being from 90:10 to 5:95.
THE TREATMENT OF AQUEOUS SYSTEMS
A method of inhibiting corrosion in an aqueous system is described which comprises adding to the system at least one water soluble inorganic nitrite and at least one phosphonate which contains at least two acid groups which are carboxylic and phosphonic acid groups such that at least one acid group is a carboxylic acid group and at least one acid group is a phosphonic acid group, at least the said two acid groups being attached to carbon atoms, the concentration of phosphonate exceeding 5 ppm weight per volume and the weight ratio of nitrite to phosphonate being from 90:10 to 5:95.
Description
-12~162~
THE TREATMENT OF AQUEOUS SYSTEMS
The present invention relates to the tre3tment of aqueous systems and, more particularly, to reducing or eliminating corrosion in aqueous systems.
Many different types of material have been employed to prevent corrosion in aqueous systems. ~hese include inorganic salts such as nitrites and chromates, inorganic mono- and polyphosphates and certain water-soluble polymers including naturally occurring materials such as lignins and starches as well as synthetic materials such as polyacrylates.
Particular problems arise in cooling systems which are subject to intermittent operation or periodic shut-down. This is because the majority of corrosion inhibitors and the like only function effectively when the cooling system is in motion. Indeed, the only materials which have so far proved to be at all effective for systems involviny periodic shut-down are the nitrites and, to a less extent, the chromates. Unfortunately, however, while nitrites are effective they have to be used in quite hi~h concentrations; amounts as much às 1000 ppm are not uncommon. Such amounts present disposal ,~, 12116~
problems because these inorganic nitrites are quite toxic. Thus the maximum nitrogen content permitted by the World Health Organisation in drinking water is equivalent to only 45 mg/l of sodium nitrite.
However, such qua:~tities of nitrite are ineffective for use as a corrosion inhibita,r in cooling systems subject to intermitt~nt operation.
It has now been found, according to the present invention, that it is possible to obtain effective corrosion inhibition if an inorganic nitrite, even in "non-toxic" amounts, that is to say less than 45 ppm, is used in com~ination in speci~ic proportions and concentrations with a particular class of phosphonate. In fact, a synergistic effect has surprisingly been found.
According to the present invention there is provided a method of controlling inhibition in aqueous systems which comprises adding to the aqueous system at least one water soluble inorganic nitrite and at least one phosphonate as defined below, the concentration of phosphonate exceeding 5 ppm (wt/volume e.g. S mg/litre) and the weight ratio oi nitrite to phosphonate being from 90:10 to 5:95, in general from 80:20 to 10:90.
Preferred ratios are between 5:1 to 2:1, especially 4.5:1 to 3:1, and most especially about 4:1.
This combination is particularly useful where very corrosive conditions exist in the cooling system, for ~21 ~ 6Z4 example in base exchanged water and very low water hardness systems.
The phosphonates for use in the present invention are those which contain at least 2 acid groups which are carboxylic and phosphonic alcid groups, such that at least one acid group is a carboxylic acid group and at least one acid group is a phosph~nic acid group, at least the said 2 acid groups being attached to carbon atoms.
The preferred pha,sphonates possess the general formula:
Il I
(~O)2P - C - COOH
CH2 ~ COOH
wherein R is hydrogen, alkyl, alkenyl or alkynyl having up to 4 carbon atoms; phenyl, cycloalkyl having 3 to 6 carbon atoms, benzyl; phenethyl or Rl R"
CH CH R " ' wherein R' is hydrogen, alkyl having 1 to 4 carbon atoms or carboxyl, R" is hydrogen or methyl and R'l' is carboxyl or phospllonate. 2-Phosphonobutane-1,2,4-tricarboxylic acid, a commercially available material, is particularly preferred. Another preferred material is 2,4-diphosphono-butane-1,2-dicarboxylic acid. These phosphonates can be obtained by processes well known in the art, for example lZ~16~4 as des~ribed in British Specification No 1 282 078.
While it is possible to add the materials separately it will generally be more convenient to incorporate them together :in the form of a composition.
Accordingly, the present invention also provides a composition suitable for addition to water to reduce or prevent corrosion which comprises at least one water soluble inorganic nitrite and at lea~t one phosphonate as defined above, the weight ratio of nitrite to phosphonate being from 90::L0 to 5:95, with the proviso that if the said ratio is from 90:10 to 5:1 the compo~ition also contains at least one other water treatment additive.
Typically, the water-soluble nitrite is sodium nitrite but other alkali metal nitrites and also calcium nitrite are also suitable~
As indicated above, by incorporating the specified phosphonate with the inorganic nitrite in the specified amounts it is possible to obtain effective corrosion inhibition even though the concentration of nitrite is less than 45 ppm. Indeed, amounts as little as 10 ppm have been found to be effective. Preferably, the nitrite is present in the system in an amount from 10 to 45 ppm especially 30 to 45 ppm, and most pr~ferably about 45 ppm. It will be appreciated, though, that in situations where health is not a factor concentrations ~Z~Z4 of up to 50 ppm or even, say, 100 ppm can be useful.
The amount of phosphonate used will generally be less than that of the nitrite in order to keep costs down and, in general, amoun*s above 5 up to 50 ppm, particularly up to 30 ppm are suitable, amounts from 10 to 15 ppm, especially about :L2 ppm, being preferred, thereby keeping down the phosphorus content in the water so as to reduce disposal problems. Amounts~ in excess of about 30 ppm are generally commercially unviable.
Phosphonates other than those of formula (I), in general, do not provide advantageous results and should, therefore, generally not be used in the system.
It has further been found that the presence of a water-soluble organic polymer in the system can further inhibit corrosion and, indeed, in certain cases an additional synergistic effect is found.
In general, the polymers suitable for use in the present invention are vinyl addition products possessing recurring units of the general formula:
Rl H
~ C - C
Z X
wherein Rl represents hydrogen or alkyl of 1 to 4 carbon atoms, X represents COOH and Z represents hydrogen or COOH or X and Z together represent -CO-0-Co-, The preferred polymers are those of methacrylic acid i.e. where Rl is methyl and z is hydrogen and acrylic acid i.e. where Rl and Z are both hydrogen. In addition phosphinopoly--acrylates and methacrylates can be used, these materials can be obtained by polymerisati.on of (meth)acrylic acid with hypo-phosphorous ,acid. In general, the molecular weight of the polymers is from 500 tc, 100 000 and the preferred polymethacrylic acid has a molecular weight of about 5 000 and the preferred pol.yacrylic acid a molecular weight of about 1 000. It will, c,f course, be appreciated that thP polymers used may be copolymers containing recurring units derived from other vinyl monomers.
Not only does the presence of polymer further reduce corrosion but since the polymers are, in general, less expensive than the phosphonates used, by incorporating polymer and, in particular, by replacing some of the phosphonate by polymer it is possible further to reduce the cost of the additives. Of course, the polymer can be added to the system separately but it will, in general, be incorporated in a composition with the nitrite and phosphonate.
Although the formulae of the phosphonate and polymer have been given in terms of the free acid it is to be understood that these materials can be used in the form of an inorganic or or~anic salt, in partio~ar an alkali metal salt such as sodium or potassium, ammonium or 12~:~L624 a lower amine salt as well as zinc or other salts. In general, however, the use of alkali metal salts is preferred.
Typically, the polymer is used in an amount from 0.5 to 50 pp!m, the preferred amount being from
THE TREATMENT OF AQUEOUS SYSTEMS
The present invention relates to the tre3tment of aqueous systems and, more particularly, to reducing or eliminating corrosion in aqueous systems.
Many different types of material have been employed to prevent corrosion in aqueous systems. ~hese include inorganic salts such as nitrites and chromates, inorganic mono- and polyphosphates and certain water-soluble polymers including naturally occurring materials such as lignins and starches as well as synthetic materials such as polyacrylates.
Particular problems arise in cooling systems which are subject to intermittent operation or periodic shut-down. This is because the majority of corrosion inhibitors and the like only function effectively when the cooling system is in motion. Indeed, the only materials which have so far proved to be at all effective for systems involviny periodic shut-down are the nitrites and, to a less extent, the chromates. Unfortunately, however, while nitrites are effective they have to be used in quite hi~h concentrations; amounts as much às 1000 ppm are not uncommon. Such amounts present disposal ,~, 12116~
problems because these inorganic nitrites are quite toxic. Thus the maximum nitrogen content permitted by the World Health Organisation in drinking water is equivalent to only 45 mg/l of sodium nitrite.
However, such qua:~tities of nitrite are ineffective for use as a corrosion inhibita,r in cooling systems subject to intermitt~nt operation.
It has now been found, according to the present invention, that it is possible to obtain effective corrosion inhibition if an inorganic nitrite, even in "non-toxic" amounts, that is to say less than 45 ppm, is used in com~ination in speci~ic proportions and concentrations with a particular class of phosphonate. In fact, a synergistic effect has surprisingly been found.
According to the present invention there is provided a method of controlling inhibition in aqueous systems which comprises adding to the aqueous system at least one water soluble inorganic nitrite and at least one phosphonate as defined below, the concentration of phosphonate exceeding 5 ppm (wt/volume e.g. S mg/litre) and the weight ratio oi nitrite to phosphonate being from 90:10 to 5:95, in general from 80:20 to 10:90.
Preferred ratios are between 5:1 to 2:1, especially 4.5:1 to 3:1, and most especially about 4:1.
This combination is particularly useful where very corrosive conditions exist in the cooling system, for ~21 ~ 6Z4 example in base exchanged water and very low water hardness systems.
The phosphonates for use in the present invention are those which contain at least 2 acid groups which are carboxylic and phosphonic alcid groups, such that at least one acid group is a carboxylic acid group and at least one acid group is a phosph~nic acid group, at least the said 2 acid groups being attached to carbon atoms.
The preferred pha,sphonates possess the general formula:
Il I
(~O)2P - C - COOH
CH2 ~ COOH
wherein R is hydrogen, alkyl, alkenyl or alkynyl having up to 4 carbon atoms; phenyl, cycloalkyl having 3 to 6 carbon atoms, benzyl; phenethyl or Rl R"
CH CH R " ' wherein R' is hydrogen, alkyl having 1 to 4 carbon atoms or carboxyl, R" is hydrogen or methyl and R'l' is carboxyl or phospllonate. 2-Phosphonobutane-1,2,4-tricarboxylic acid, a commercially available material, is particularly preferred. Another preferred material is 2,4-diphosphono-butane-1,2-dicarboxylic acid. These phosphonates can be obtained by processes well known in the art, for example lZ~16~4 as des~ribed in British Specification No 1 282 078.
While it is possible to add the materials separately it will generally be more convenient to incorporate them together :in the form of a composition.
Accordingly, the present invention also provides a composition suitable for addition to water to reduce or prevent corrosion which comprises at least one water soluble inorganic nitrite and at lea~t one phosphonate as defined above, the weight ratio of nitrite to phosphonate being from 90::L0 to 5:95, with the proviso that if the said ratio is from 90:10 to 5:1 the compo~ition also contains at least one other water treatment additive.
Typically, the water-soluble nitrite is sodium nitrite but other alkali metal nitrites and also calcium nitrite are also suitable~
As indicated above, by incorporating the specified phosphonate with the inorganic nitrite in the specified amounts it is possible to obtain effective corrosion inhibition even though the concentration of nitrite is less than 45 ppm. Indeed, amounts as little as 10 ppm have been found to be effective. Preferably, the nitrite is present in the system in an amount from 10 to 45 ppm especially 30 to 45 ppm, and most pr~ferably about 45 ppm. It will be appreciated, though, that in situations where health is not a factor concentrations ~Z~Z4 of up to 50 ppm or even, say, 100 ppm can be useful.
The amount of phosphonate used will generally be less than that of the nitrite in order to keep costs down and, in general, amoun*s above 5 up to 50 ppm, particularly up to 30 ppm are suitable, amounts from 10 to 15 ppm, especially about :L2 ppm, being preferred, thereby keeping down the phosphorus content in the water so as to reduce disposal problems. Amounts~ in excess of about 30 ppm are generally commercially unviable.
Phosphonates other than those of formula (I), in general, do not provide advantageous results and should, therefore, generally not be used in the system.
It has further been found that the presence of a water-soluble organic polymer in the system can further inhibit corrosion and, indeed, in certain cases an additional synergistic effect is found.
In general, the polymers suitable for use in the present invention are vinyl addition products possessing recurring units of the general formula:
Rl H
~ C - C
Z X
wherein Rl represents hydrogen or alkyl of 1 to 4 carbon atoms, X represents COOH and Z represents hydrogen or COOH or X and Z together represent -CO-0-Co-, The preferred polymers are those of methacrylic acid i.e. where Rl is methyl and z is hydrogen and acrylic acid i.e. where Rl and Z are both hydrogen. In addition phosphinopoly--acrylates and methacrylates can be used, these materials can be obtained by polymerisati.on of (meth)acrylic acid with hypo-phosphorous ,acid. In general, the molecular weight of the polymers is from 500 tc, 100 000 and the preferred polymethacrylic acid has a molecular weight of about 5 000 and the preferred pol.yacrylic acid a molecular weight of about 1 000. It will, c,f course, be appreciated that thP polymers used may be copolymers containing recurring units derived from other vinyl monomers.
Not only does the presence of polymer further reduce corrosion but since the polymers are, in general, less expensive than the phosphonates used, by incorporating polymer and, in particular, by replacing some of the phosphonate by polymer it is possible further to reduce the cost of the additives. Of course, the polymer can be added to the system separately but it will, in general, be incorporated in a composition with the nitrite and phosphonate.
Although the formulae of the phosphonate and polymer have been given in terms of the free acid it is to be understood that these materials can be used in the form of an inorganic or or~anic salt, in partio~ar an alkali metal salt such as sodium or potassium, ammonium or 12~:~L624 a lower amine salt as well as zinc or other salts. In general, however, the use of alkali metal salts is preferred.
Typically, the polymer is used in an amount from 0.5 to 50 pp!m, the preferred amount being from
2 to 10 ppm.
It will be appreciated that other 1~ toxic materials conventionally us,ed in water treatment can be added to the system and/or the composition including silicates, inorganic phosphates and polyphosphates and lignin derivatives as well as heterocyclic compounds for corrosion inhibition of yellow metals, such as benzo-triazole, tolyltriazole and mercaptobenzothiazole.
The compositions of the present invention will normally be in the form of an aqueous solution but other possible forms include powders and briquettes.
Typically the solutions will contain 20 to 50 weight percent, es,pecially 25 to 35 weight percent, nitrite, 2.5 to 20 weight percent, especially 5 to 10 weight percent, 2~ phosphonate and, optionally, 1 to 10 weight percent, especially 1.5 to 3 weight percent, polymer. Concentrations - of other additives, such as benzotriazole, which can be present, are suitably from 0.1 to 5 weight percent, especially 0.5 to l.S weight percent; in order-to bring the benzotriazole into solution the pH sho~lld be increased to, say, 12 to 12.5 with caustic soda. A particularly lZ~6Z~
preferred fonmulation contains: 30 weight % sodium nitrite, 16 weight % 2-phosphonobutane-1,2,4-tricarboxylic acid (50% active), 5 weight % polyacrylic acid (33% active) and 1 weight % benzotriazole with sufficient caustic! soda to ]bring the pH of the aqueous solution to 12 to 12.5. Naturally the amount of the formulation used will depend upon the nature of the system and o~ the water but with t]nis specific formulation amounts from 100 to 200, especially 150 to 200,ppm are generally suitable.
The following examples further illustrate the present invention. In these examples two different types of tests were employed, namely a circulatory test and a test to simulate intermittent flow operations.
In the circulatory test a laboratory test apparatus was used in which water is circulated etc by means of a pump from a reservoir maintained at a temperature of 54C with a heater and thermostat. The water passes through a glass tube assembly holding the metal test specimens (flow rate 2 ft/sec) and then is returned to the reservoir entraining air as it does so in order - to keep the water saturated with oxygen as it would be in a typical open recirculating cooling system.
Water lost by evaporation tconcentrat-ion factor 1.7) is replaced from an elevated tank through a float control to maintain a constant volume in the system.
~Z~l~;Z~
_ g _ In each test treatment is applied at three times normal dose for 24 hours in order to passivate the metals, then the water is diluted to the normal dose for the remainder of the test. Each test is for a minimum of
It will be appreciated that other 1~ toxic materials conventionally us,ed in water treatment can be added to the system and/or the composition including silicates, inorganic phosphates and polyphosphates and lignin derivatives as well as heterocyclic compounds for corrosion inhibition of yellow metals, such as benzo-triazole, tolyltriazole and mercaptobenzothiazole.
The compositions of the present invention will normally be in the form of an aqueous solution but other possible forms include powders and briquettes.
Typically the solutions will contain 20 to 50 weight percent, es,pecially 25 to 35 weight percent, nitrite, 2.5 to 20 weight percent, especially 5 to 10 weight percent, 2~ phosphonate and, optionally, 1 to 10 weight percent, especially 1.5 to 3 weight percent, polymer. Concentrations - of other additives, such as benzotriazole, which can be present, are suitably from 0.1 to 5 weight percent, especially 0.5 to l.S weight percent; in order-to bring the benzotriazole into solution the pH sho~lld be increased to, say, 12 to 12.5 with caustic soda. A particularly lZ~6Z~
preferred fonmulation contains: 30 weight % sodium nitrite, 16 weight % 2-phosphonobutane-1,2,4-tricarboxylic acid (50% active), 5 weight % polyacrylic acid (33% active) and 1 weight % benzotriazole with sufficient caustic! soda to ]bring the pH of the aqueous solution to 12 to 12.5. Naturally the amount of the formulation used will depend upon the nature of the system and o~ the water but with t]nis specific formulation amounts from 100 to 200, especially 150 to 200,ppm are generally suitable.
The following examples further illustrate the present invention. In these examples two different types of tests were employed, namely a circulatory test and a test to simulate intermittent flow operations.
In the circulatory test a laboratory test apparatus was used in which water is circulated etc by means of a pump from a reservoir maintained at a temperature of 54C with a heater and thermostat. The water passes through a glass tube assembly holding the metal test specimens (flow rate 2 ft/sec) and then is returned to the reservoir entraining air as it does so in order - to keep the water saturated with oxygen as it would be in a typical open recirculating cooling system.
Water lost by evaporation tconcentrat-ion factor 1.7) is replaced from an elevated tank through a float control to maintain a constant volume in the system.
~Z~l~;Z~
_ g _ In each test treatment is applied at three times normal dose for 24 hours in order to passivate the metals, then the water is diluted to the normal dose for the remainder of the test. Each test is for a minimum of
3 days, the test specimens being cleaned before and after each run to find the weight: loss which is then calculated to show the average corrosiLon rate in mils (0.025 mm) per year.
The water used in the tests was Widnes mains water, 75 ppm calcium har~less, 90 ppm. M. alkalinity.
In the following tests the combined dosage of additives in the system was 30 ppm. "In line" or "High flow" represents the corrosion rate in the tube while "low flow/static areas" represents the corrosion rate in the body of the reservoir.
The results clearly show that the chosen phosphonates in combination with the nitrite do exhibit synergism.
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- lZ116Z4 Further tests were carried out in a similar manner, with the following results:
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The water used in the tests was Widnes mains water, 75 ppm calcium har~less, 90 ppm. M. alkalinity.
In the following tests the combined dosage of additives in the system was 30 ppm. "In line" or "High flow" represents the corrosion rate in the tube while "low flow/static areas" represents the corrosion rate in the body of the reservoir.
The results clearly show that the chosen phosphonates in combination with the nitrite do exhibit synergism.
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- lZ116Z4 Further tests were carried out in a similar manner, with the following results:
~2~1624 __ ... __ ~ _ ,_ U) u~ In t~--- 1~1 ~ U'l t'~l t~l N
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- -
Claims (27)
1. A method of controlling corrosion in an aqueous system which comprises adding to the system at least one water soluble inorganic nitrite and at least one phosphonate having the general formula:
wherein R is hydrogen, alkyl, alkenyl or alkynyl having up to 4 carbon atoms; phenyl; cycloalkyl having 3 to 6 carbon atoms: benzyl; phenethyl or wherein R' is hydrogen, alkyl having 1 to 4 carbon atoms or carboxyl, R" is hydrogen or methyl and R''' is carboxyl or phosphonate, the concentration of phosphonate exceeding 5 ppm weight per volume and the weight ratio of nitrite to phosphonate being from 2:1 to 1:5.
wherein R is hydrogen, alkyl, alkenyl or alkynyl having up to 4 carbon atoms; phenyl; cycloalkyl having 3 to 6 carbon atoms: benzyl; phenethyl or wherein R' is hydrogen, alkyl having 1 to 4 carbon atoms or carboxyl, R" is hydrogen or methyl and R''' is carboxyl or phosphonate, the concentration of phosphonate exceeding 5 ppm weight per volume and the weight ratio of nitrite to phosphonate being from 2:1 to 1:5.
2. A method according to claim 1 in which the aqueous system is a base exchanged water or a water of very low water hardness.
3. A method according to claim 1 or 2 in which the phosphonate is 2-phosphonobutane-1,2,4-tricarboxylic acid or 2,4-diphosphonobutane-1,2-dicarboxylic acid or a salt thereof.
4. A method according to claim 1 or 2 in which the concentration of nitrite is less than 45 ppm weight per volume.
5. A method according to claim 1 or 2 in which the concentration of nitrite is from 10 to less than 45 ppm.
6. A method according to claim 1 or 2 in which the concentration of phosphonate is from 10 to 15 ppm weight per volume.
7. A method according to claim 1 or 2 which comprises adding also a water soluble organic polymer.
8. A method according to claim 1 or 2 which comprises adding also a water soluble organic polymer which possesses recurring units of the general formula:
wherein R1 represents hydrogen or alkyl of 1 to 4 carbon atoms, X represents COOH and z represents hydrogen or COOH
or X and Z together represent -CO-O-CO-.
wherein R1 represents hydrogen or alkyl of 1 to 4 carbon atoms, X represents COOH and z represents hydrogen or COOH
or X and Z together represent -CO-O-CO-.
9. A method according to claim 1 or 2 which comprises adding also a water soluble polymer of acrylic or methacrylic acid.
10. A method according to claim 1 or 2 which comprises adding also a water soluble phosphinopolyacrylate or methacrylate.
11. A method according to claim 1 or 2 which comprises adding also a water soluble organic polymer which has a molecular weight from 500 to 100,000.
12. A method according to claim 1 or 2 which comprises adding also a water soluble organic polymer in an amount from 0.5 to 50 ppm weight per volume.
13. A method according to claim 1 or 2 which comprises adding also a water soluble organic polymer in an amount from 2 to 10 ppm weight per volume.
14. A composition suitable for addition to water which comprises at least one water soluble inorganic nitrite and at least one phosphonate having the general formula:
wherein R is hydrogen, alkyl, alkenyl or alkynyl having up to 4 carbon atoms; phenyl; cycloalkyl having 3 to 6 carbon atoms; benzyl; phenethyl or wherein R' is hydrogen, alkyl having 1 to 4 carbon atoms or carboxyl, R" is hydrogen or methyl and R''' is carboxyl or phosphonate, the weight ratio of nitrite to phosphonate being from 2:1 to 1:5.
wherein R is hydrogen, alkyl, alkenyl or alkynyl having up to 4 carbon atoms; phenyl; cycloalkyl having 3 to 6 carbon atoms; benzyl; phenethyl or wherein R' is hydrogen, alkyl having 1 to 4 carbon atoms or carboxyl, R" is hydrogen or methyl and R''' is carboxyl or phosphonate, the weight ratio of nitrite to phosphonate being from 2:1 to 1:5.
15. A composition according to claim 14 further comprising a silicate, an inorganic phosphate or polyphosphate, a lignin derivative, or a heterocyclic compound.
16. A composition according to claim 14 or 15 which is in the form of an aqueous solution which contains 20 to 50 weight percent of nitrite and 2.5 to 20 weight percent of phosphonate.
17. A composition according to claim 14 or 15 which is in the form of an aqueous solution which contains 25 to 35 weight percent of nitrite and 5 to 10 weight percent of phosphonate.
18. A composition according to claim 14 which also contains a water soluble organic polymer.
19. A composition according to claim 18 in which the organic polymer possesses recurring units of the general formula:
wherein R1 represents hydrogen or alkyl of 1 to 4 carbon atoms, X represents COOH and Z represents hydrogen or COOH
or X and Z together represents -CO-O-CO-.
wherein R1 represents hydrogen or alkyl of 1 to 4 carbon atoms, X represents COOH and Z represents hydrogen or COOH
or X and Z together represents -CO-O-CO-.
20. A composition according to claim 14 or 15 which also contains 1 to 10 weight percent of a water soluble organic polymer.
21. A composition according to claim 14 or 15 which also contains 1.5 to 3 weight percent of a water soluble organic polymer.
22. A composition according to claim 14 which is an aqueous solution which comprises 30 weight percent sodium nitrite, 8 weight percent 2-phosphonobutane-1,2,4-tricaxboxylic acid, 1 2/3 weight percent polyacrylic acid and 1 weight percent benzotriazole, the composition being adjusted to a pH of 12 to 12.5 with caustic soda.
23. A method according to claim 1 or 2 in which the weight ratio of nitrite to phosphonate is from 1:2 to 1:5.
24. A method according to claim 1 or 2 in which the concentration of the nitrite is less than 45 ppm.
25. A method according to claim 1 or 2 in which the aqueous system is a cooling system.
26. A composition according to claim 14 in which the weight ratio of nitrite to phosphonate is from 1:2 to 1:5.
27. A composition according to claim 14 in which said phosphonate is 2-phosphonobutane-1,2,4-tricarboxylic acid or 2,4-diphosphonobutane-1,2-dicarboxylic acid or a salt thereof.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB08211321A GB2118159B (en) | 1982-04-20 | 1982-04-20 | The treatment of aqueous systems |
| GB8211321 | 1982-04-20 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1211624A true CA1211624A (en) | 1986-09-23 |
Family
ID=10529783
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000425925A Expired CA1211624A (en) | 1982-04-20 | 1983-04-15 | Treatment of aqueous systems |
Country Status (10)
| Country | Link |
|---|---|
| JP (1) | JPS58189380A (en) |
| CA (1) | CA1211624A (en) |
| DE (1) | DE3314008A1 (en) |
| ES (1) | ES521607A0 (en) |
| FR (1) | FR2525241B1 (en) |
| GB (1) | GB2118159B (en) |
| IT (1) | IT1164190B (en) |
| MY (1) | MY8600404A (en) |
| PH (1) | PH19173A (en) |
| SE (1) | SE8302161L (en) |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2168359B (en) * | 1984-11-08 | 1988-05-05 | Grace W R & Co | A method of inhibiting corrosion in aqueous systems |
| CA1332138C (en) * | 1985-10-29 | 1994-09-27 | Brian Greaves | Treatment of aqueous systems |
| GB2184109A (en) * | 1985-10-29 | 1987-06-17 | Grace W R & Co | The treatment of aqueous systems |
| GB9027921D0 (en) * | 1990-12-21 | 1991-02-13 | D D D Limited | Descaling composition |
| DE4331910C2 (en) * | 1993-09-20 | 1997-05-28 | Aisan Ind | Reciprocating fluid pump |
| WO2000039359A1 (en) * | 1998-12-29 | 2000-07-06 | Calgon Corporation | Corrosion inhibitor compositions and methods to control metal corrosion in brine systems |
| US9994755B2 (en) | 2012-09-07 | 2018-06-12 | Prestone Products Corporation | Heat transfer fluids and corrosion inhibitor formulations for use thereof |
| US8617416B1 (en) * | 2012-09-07 | 2013-12-31 | Prestone Products Corporation | Heat transfer fluids and corrosion inhibitor formulations for use thereof |
| JP2017088993A (en) * | 2015-11-17 | 2017-05-25 | 三浦工業株式会社 | Anticorrosive water treatment agent and anticorrosive method |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1392044A (en) * | 1971-06-26 | 1975-04-23 | Ciba Geigy Ag | Corrosion inhibiting composition |
| DE2225645A1 (en) * | 1972-05-26 | 1974-01-17 | Bayer Ag | PROCESS FOR PREVENTING CORROSION AND STONE SETTING IN WATER SYSTEMS |
| US4052160A (en) * | 1975-07-23 | 1977-10-04 | Ciba-Geigy Corporation | Corrosion inhibitors |
| GB2084128B (en) * | 1980-09-25 | 1983-11-16 | Dearborn Chemicals Ltd | Inhibiting corrosion in aqueous systems |
-
1982
- 1982-04-20 GB GB08211321A patent/GB2118159B/en not_active Expired
-
1983
- 1983-04-15 CA CA000425925A patent/CA1211624A/en not_active Expired
- 1983-04-18 DE DE19833314008 patent/DE3314008A1/en not_active Withdrawn
- 1983-04-18 PH PH28786A patent/PH19173A/en unknown
- 1983-04-18 SE SE8302161A patent/SE8302161L/en not_active Application Discontinuation
- 1983-04-19 FR FR8306370A patent/FR2525241B1/en not_active Expired
- 1983-04-19 JP JP58067919A patent/JPS58189380A/en active Pending
- 1983-04-19 ES ES521607A patent/ES521607A0/en active Granted
- 1983-04-19 IT IT20678/83A patent/IT1164190B/en active
-
1986
- 1986-12-30 MY MY404/86A patent/MY8600404A/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| PH19173A (en) | 1986-01-16 |
| IT1164190B (en) | 1987-04-08 |
| ES8406391A1 (en) | 1984-07-01 |
| ES521607A0 (en) | 1984-07-01 |
| DE3314008A1 (en) | 1983-10-20 |
| MY8600404A (en) | 1986-12-31 |
| SE8302161D0 (en) | 1983-04-18 |
| SE8302161L (en) | 1983-10-21 |
| JPS58189380A (en) | 1983-11-05 |
| GB2118159B (en) | 1985-09-04 |
| FR2525241A1 (en) | 1983-10-21 |
| FR2525241B1 (en) | 1987-05-07 |
| IT8320678A0 (en) | 1983-04-19 |
| GB2118159A (en) | 1983-10-26 |
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