US2515529A - Corrosion inhibiting compositions and method - Google Patents
Corrosion inhibiting compositions and method Download PDFInfo
- Publication number
- US2515529A US2515529A US685379A US68537946A US2515529A US 2515529 A US2515529 A US 2515529A US 685379 A US685379 A US 685379A US 68537946 A US68537946 A US 68537946A US 2515529 A US2515529 A US 2515529A
- Authority
- US
- United States
- Prior art keywords
- water
- per gallon
- corrosion
- range
- cyanide
- 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 - Lifetime
Links
- 238000005260 corrosion Methods 0.000 title claims description 55
- 230000007797 corrosion Effects 0.000 title claims description 55
- 239000000203 mixture Substances 0.000 title claims description 29
- 230000002401 inhibitory effect Effects 0.000 title claims description 28
- 238000000034 method Methods 0.000 title description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 93
- 229920000388 Polyphosphate Polymers 0.000 claims description 35
- 239000001205 polyphosphate Substances 0.000 claims description 35
- 235000011176 polyphosphates Nutrition 0.000 claims description 35
- 229910019142 PO4 Inorganic materials 0.000 claims description 30
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 claims description 28
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 claims description 25
- 239000010452 phosphate Substances 0.000 claims description 24
- 229910021432 inorganic complex Inorganic materials 0.000 claims description 4
- 235000013339 cereals Nutrition 0.000 description 50
- 235000021317 phosphate Nutrition 0.000 description 27
- -1 ferrous metals Chemical class 0.000 description 9
- 229910052751 metal Inorganic materials 0.000 description 8
- 239000002184 metal Substances 0.000 description 8
- 239000000276 potassium ferrocyanide Substances 0.000 description 8
- XOGGUFAVLNCTRS-UHFFFAOYSA-N tetrapotassium;iron(2+);hexacyanide Chemical compound [K+].[K+].[K+].[K+].[Fe+2].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-] XOGGUFAVLNCTRS-UHFFFAOYSA-N 0.000 description 8
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 7
- 239000000126 substance Substances 0.000 description 7
- FQENQNTWSFEDLI-UHFFFAOYSA-J sodium diphosphate Chemical compound [Na+].[Na+].[Na+].[Na+].[O-]P([O-])(=O)OP([O-])([O-])=O FQENQNTWSFEDLI-UHFFFAOYSA-J 0.000 description 6
- 235000019818 tetrasodium diphosphate Nutrition 0.000 description 6
- KXZJHVJKXJLBKO-UHFFFAOYSA-N chembl1408157 Chemical compound N=1C2=CC=CC=C2C(C(=O)O)=CC=1C1=CC=C(O)C=C1 KXZJHVJKXJLBKO-UHFFFAOYSA-N 0.000 description 5
- 235000019820 disodium diphosphate Nutrition 0.000 description 5
- GYQBBRRVRKFJRG-UHFFFAOYSA-L disodium pyrophosphate Chemical compound [Na+].[Na+].OP([O-])(=O)OP(O)([O-])=O GYQBBRRVRKFJRG-UHFFFAOYSA-L 0.000 description 5
- RHSBIGNQEIPSCT-UHFFFAOYSA-N stearonitrile Chemical compound CCCCCCCCCCCCCCCCCC#N RHSBIGNQEIPSCT-UHFFFAOYSA-N 0.000 description 5
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 229910001209 Low-carbon steel Inorganic materials 0.000 description 4
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 150000002825 nitriles Chemical class 0.000 description 4
- GTSHREYGKSITGK-UHFFFAOYSA-N sodium ferrocyanide Chemical compound [Na+].[Na+].[Na+].[Na+].[Fe+2].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-] GTSHREYGKSITGK-UHFFFAOYSA-N 0.000 description 4
- 239000000264 sodium ferrocyanide Substances 0.000 description 4
- 235000012247 sodium ferrocyanide Nutrition 0.000 description 4
- 239000003643 water by type Substances 0.000 description 4
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 3
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 3
- 238000009835 boiling Methods 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- VEJCUEBBRSCJRP-UHFFFAOYSA-L calcium;hydron;phosphonato phosphate Chemical compound [Ca+2].OP(O)(=O)OP([O-])([O-])=O VEJCUEBBRSCJRP-UHFFFAOYSA-L 0.000 description 3
- XEYBHCRIKKKOSS-UHFFFAOYSA-N disodium;azanylidyneoxidanium;iron(2+);pentacyanide Chemical compound [Na+].[Na+].[Fe+2].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].[O+]#N XEYBHCRIKKKOSS-UHFFFAOYSA-N 0.000 description 3
- CBWRQUSMBGHKFO-UHFFFAOYSA-H hexasodium [[dioxidophosphinothioyloxy(oxido)phosphinothioyl]oxy-oxidophosphinothioyl] phosphate Chemical compound [O-]P([O-])(=S)OP(=S)([O-])OP(=S)([O-])OP(=O)([O-])[O-].[Na+].[Na+].[Na+].[Na+].[Na+].[Na+] CBWRQUSMBGHKFO-UHFFFAOYSA-H 0.000 description 3
- TVHALOSDPLTTSR-UHFFFAOYSA-H hexasodium;[oxido-[oxido(phosphonatooxy)phosphoryl]oxyphosphoryl] phosphate Chemical compound [Na+].[Na+].[Na+].[Na+].[Na+].[Na+].[O-]P([O-])(=O)OP([O-])(=O)OP([O-])(=O)OP([O-])([O-])=O TVHALOSDPLTTSR-UHFFFAOYSA-H 0.000 description 3
- 229910052700 potassium Inorganic materials 0.000 description 3
- 239000011591 potassium Substances 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- 229940083618 sodium nitroprusside Drugs 0.000 description 3
- 235000019832 sodium triphosphate Nutrition 0.000 description 3
- DCXPBOFGQPCWJY-UHFFFAOYSA-N trisodium;iron(3+);hexacyanide Chemical compound [Na+].[Na+].[Na+].[Fe+3].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-].N#[C-] DCXPBOFGQPCWJY-UHFFFAOYSA-N 0.000 description 3
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- GCLGEJMYGQKIIW-UHFFFAOYSA-H sodium hexametaphosphate Chemical compound [Na]OP1(=O)OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])O1 GCLGEJMYGQKIIW-UHFFFAOYSA-H 0.000 description 2
- 235000019982 sodium hexametaphosphate Nutrition 0.000 description 2
- 239000008399 tap water Substances 0.000 description 2
- 235000020679 tap water Nutrition 0.000 description 2
- 239000001577 tetrasodium phosphonato phosphate Substances 0.000 description 2
- 229920001342 Bakelite® Polymers 0.000 description 1
- 239000004484 Briquette Substances 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000003619 algicide Substances 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 150000004645 aluminates Chemical class 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 239000003899 bactericide agent Substances 0.000 description 1
- 239000004637 bakelite Substances 0.000 description 1
- 239000001506 calcium phosphate Substances 0.000 description 1
- 229910000389 calcium phosphate Inorganic materials 0.000 description 1
- 235000011010 calcium phosphates Nutrition 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000005536 corrosion prevention Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- BNIILDVGGAEEIG-UHFFFAOYSA-L disodium hydrogen phosphate Chemical compound [Na+].[Na+].OP([O-])([O-])=O BNIILDVGGAEEIG-UHFFFAOYSA-L 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 230000000979 retarding effect Effects 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 108010080511 serum sodium transport inhibitor Proteins 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 235000017550 sodium carbonate Nutrition 0.000 description 1
- MNWBNISUBARLIT-UHFFFAOYSA-N sodium cyanide Chemical compound [Na+].N#[C-] MNWBNISUBARLIT-UHFFFAOYSA-N 0.000 description 1
- AJPJDKMHJJGVTQ-UHFFFAOYSA-M sodium dihydrogen phosphate Chemical compound [Na+].OP(O)([O-])=O AJPJDKMHJJGVTQ-UHFFFAOYSA-M 0.000 description 1
- 239000001488 sodium phosphate Substances 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 description 1
- RYFMWSXOAZQYPI-UHFFFAOYSA-K trisodium phosphate Chemical compound [Na+].[Na+].[Na+].[O-]P([O-])([O-])=O RYFMWSXOAZQYPI-UHFFFAOYSA-K 0.000 description 1
- 229910000406 trisodium phosphate Inorganic materials 0.000 description 1
- 235000019801 trisodium phosphate Nutrition 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
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
- C23F11/18—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 using inorganic inhibitors
- C23F11/187—Mixtures of inorganic inhibitors
- C23F11/188—Mixtures of inorganic inhibitors containing phosphates
Definitions
- This invention relates to new and improved corrosion inhibiting compositions'and to a new and improved method of inhibiting corrosion.
- the invention is particularly concerned with corrosion inhibiting compositions for preventing or inhibiting underwater corrosion in systems where water is moving, as through condensers, engine jackets, spray or cooling towers, and distribution systems.
- the invention is especially valuable in inhibitin corrosion of ferrous metals, including iron and steel.
- phosphates will inhibit underwater corrosion on ferrous metals under certain conditions.
- the dosage of the phosphate will vary depending upon such factors as the velocity of the water, the temperature and the chemical content of the water. Some phosphates are more efiective than others in certain types of waters. Thus, if the water contains very much calcium the use or an orthophosphate is undesirable because the calcium phosphate scale is deposited in the pipes and tubes, thereby producing a result which may be worse than the corrosion.
- the corroding tendency of the water is greatly increased by the presence of sodium chloride and sodium sulfate. As the velocity of the water increases the dosage of phosphate required to inhibit corrosion normally decreases, and as the temperature of the water is increased the dosage of phosphate to inhibit corrosion also increases.
- One of the objects of this invention is to provide new and improved corrosion inhibiting compositions.
- a further object of the invention is to produce new and improved corrosion inhibiting compositions which are eilective in preventing or retarding the corrosive efiects of relatively corrosive waters on ferrous metals at relatively high temperatures.
- Another object of the invention is to provide a new and improved method for inhibiting corrosion.
- a still further object of the invention is to proi 2 vide a new and improved method of inhibiting corrosion by a chemical treatment involving the utilization of relati ely small amounts of corrosion inhibiting chemicals.
- new and improved corrosion inhibiting compositions are prepared by intimately mixing or blending a corrosion inhibiting phosphate with a compound containing a CN group, preferably a complex inorganic cyanide, with or without the addition of binders, algicides, bactericides and/or other water treating chemicals.
- a corrosion inhibiting phosphate with a compound containing a CN group, preferably a complex inorganic cyanide, with or without the addition of binders, algicides, bactericides and/or other water treating chemicals.
- a corrosion inhibiting phosphate with a compound containing a CN group, preferably a complex inorganic cyanide, with or without the addition of binders, algicides, bactericides and/or other water treating chemicals.
- sodium ferrocyanide, sodium nitroprusside (NaaFe(CN) 5NO.2H20) potassium ferrocyanide, sodium ferricyanide and/or potassium ierricyanide in conjunction with a poly
- a corrosive water was prepared as previously described by mixing Chicago tap water and distilled water in the ratio of 1:1 by weight and per gallon then adding 10.0 grains of sodium chlocorrosion protection at a temperature of 180 deride. This water was then used in various tests on SAE-1020 mild steel. The. tests were conducted by mounting a rod of BAE-l020 mild steel in a non-conducting mounting of Bakelite or rubber on a variable speed electric motor with the other end of the rod in the water to be tested. The velocity of the water can then be determined from the diameter of the rod and the speed at which the rod is turned by the motor. The water can be heated in any suitable manner to any desired temperature and maintained at that temperature. After each test the amount of corrosion can be determined by chemical analysis of the water for iron and by visual observation. Both methods'were used in evaluating the results hereinafter set forth.
- the following table shows the dosage in grains per gallon of NSBHZP'I required for corrosion prevention of SAE-1020 'mild steel under various conditions of temperature and water velocity.
- EXAMPLE II EXAMIPLEIII Tests made in the manner described under Example IA showed that 3.0 grains per gallon of NaoP'lOu glassy septaphosphate and 0.2 grain per gallon of sodium cyanide (NaCN) gave very good feet per second velocity.
- EXAMPLE IV This example illustrates the preparation of a corrosion inhibiting composition suitable for the practice of the invention.
- Thi composition was prepared by pulverizing and blending together grees F. and 1.9
- This composition can be used in a ball feeder for the treatment of water.
- the dosage of the cyanide need not be very high to exert a very marked effect in corrosion protection.
- the optimum amount of the cyanide is usually within the range of 0.05 to 0.5 of the phosphate, and very good results have been obtained when the amount of cyanide is around 0.33 of the amount of phosphate by weight.
- the ratio of phosphate is preferably within the range of 0.1 grain per gallon to 5 grains per gallon, and the ratio of cyanide is preferably within the range of 0.05 grain per gallon to 0.5 grain per gallon. Very excellent results have been obtained when only 0.1 grain per gallon of potassium ferrocyanide was added along with the phosphate.
- the invention is not limited to the use of any a particular type of corrosion inhibiting phosphate.
- orthophosphates can be used, as, for example, trisodium phosphate, monosodium dihydrogen phosphate and disodium monohydrogen phosphate.
- a polyphosphate including, for example, one or more of the following phosphates: sodium acid pyrophosphate, tetrasodium pyrophosphate, sodium tripolyphosphate (NaliPIiOlO), sodium tetraphosphate (Na4P6ol3), calcium acid pyrophosphate, sodium trithiotetraphosphate tially water insoluble, was also found to be eflective.
- the invention provides new and useful water treating compositions which are effective in preventing corrosion over a wide range of temperature, and in waters that are normally very corrosive when not treated.
- the invention has important advantages in providing a method of protection against corrosion by the addition of relatively small amounts of substances which do not cause other undesirable operating conditions. The use of such relatively small amounts has the added advantage of reducing the cost of corrosion protection.
- Example 13 it has been demonstrated in Example 13 that adequate corrosion protection at 180 degrees F. can be obtained with as little as 1.0 grain per gallon of glassy septaphosphate in conjunction with 0.1 grain per gallon of potassium ferricyanide, whereas, as shown by Table 1, without the addition of the cyanide, at the same water velocity the polyphosphate used did not give adequate corrosion protection when 6 grains per gallon were employed at 180 degrees F.
- a corrosion inhibiting composition comprising essentially a water soluble p lyphosphate and a water soluble inorganic complex cyanide, the ratio of said cyanide to said phosphate being within the range of 0.05 to 0.5 by weight of said phosphate, and said composition being capable of dissolving in water to give a dissolved phosphate concentration within the range of 0.1 grain per gallon to grains per gallon of water and a dissolved cyanide concentration within the range of 0.05 grain per gallon to 0.5 grain per gallon of water.
- a corrosion inhibiting composition comprising essentially a water soluble glassy polyphosphate and a water soluble inorganic complex cyanide, the ratio of said cyanide to said phosphate being within the range 01 0.05 to 0.5 by weight of said phosphate, and said composition being capable of dissolving in water to give a dissolved phosphate concentration within the range of 0.1 grain per gallon to 5 grains per gallon of water and a dissolved cyanide concentration within the range of 0.05 grain per gallon to 0.5 grain per gallon of water.
- a corrosion inhibiting composition comprising essentially a water soluble molecularly dehydrated phosphate and an alkali metal ferrocyanide, the ratio of said cyanide to said phosphate being within the range of 0.05 to 0.5 by weight oi said phosphate, and said composition being capable of dissolving in water to give a dissolved phosphate concentration within the range of 0.1 grain per gallon to 5 grains per gallon of water and a dissolved cyanide concentration within the range of 0.05 grain per gallon to 0.5 grain per gallon of water.
- a corrosion inhibiting composition comprising essentially approximately 7% of sodium terrocyanide, approximately 50% of glassy septaphosphate, and approximately 27-28% of anhydrous tetrasodium pyrophosphate.
- a method of inhibiting corrosion in water which is in contact with ferrous metals at temperatures above about degrees F. which comprises essentially incorporating with the water so that bpth are present at the same time (1) a polyphosphate and (2) a water soluble inorganic complex cyanide, the quantity of said polyphosphate in said water being within the range of 0.1 grain per gallon to 5 grains per gallon of said water, and the quantity of said inorganic cyanide in said water being within the range of 0.05 to 0.5 by weight of said polyphosphate.
- a method of inhibiting corrosion in water which is in contact with ferrous metals at temperatures above about 180 degrees F. which comprises incorporating with the water so that both are present at the same time (1) a polyphosphate and (2) a water soluble potassium ferrocyanide, the quantity of said polyphosphate in said water being within the range of 0.1 grain per gallon to 5 grains per gallon of said water, and the quantity of said ferrocyanide in said water being within the range of 0.05 to 0.5 by weight of said polyphosphate.
- a method of inhibiting corrosion in water at temperatures above about 180 degrees F. which comprises incorporating with the water so that both are present at the same time (1) a polyphosphate and (2) a water soluble potassium ferrocyanide, the quantity of polyphosphate being within the range of 1 to 5 grains per gallon, and the quantity of potassium ferrocyanide being within the range of 0.1 to 0.5 grains per gallon, the ratio of said ferrocyanide to said polyphosphate being within the range of 0.05 to 0.5 by weight of the polyphosphate.
- a corrosion inhibiting composition comprising essentially a water soluble polyphosphate from the group consisting of sodium acid pyrophosphate, tetrasodium pyrophosphate, sodium tripolyphosphate, sodium tetraphosphate, calcium acid pyrophosphate, sodium trithiotetraphosphate, sodium hexametaphosphate and glassy septaphosphate, and a cyanide from the group consisting of sodium ferrocyanide, sodium nitroprusside, potassium ferrocyanide, sodium ferricyanide, potassium ferrlcyanide, sodium cyanide and stearyl nitrile, the ratio of said cyanide to said polyphosphate being within the range of 0.05 to 0.5 by weight of said polyphosphate and said composition being capable of dissolving in water to give a dissolved polyphosphate concentration within the range of 0.1 grain per gallon to 5 grains per gallon of water and a dissolved cyanide concentration within. the range of 0.05 grain per gallon to 0.5 grain per gallon of water.
- a corrosion inhibiting composition comprising essentially a water soluble polyphosphate and sodium cyanide, the ratio of said cyanide to said polyphosphate being Within the range of 0.05 to 0.5 by weight of said polyphosphate and said composition being capable of dissolving in water to give a dissolved polyphosphate concentration within the range of 0.1 grain per gallon to 5 grains per gallon of water and a dissolved cyanide concentration within the range of 0.05 grain per gallon to 0.5 grain per gallon of water.
- a corrosion inhibiting composition comprising essentially a water soluble polyphosphate and stearyl nitrile, the ratio of said nitrile to said polyphosphate being within the range of 0.05 to 0.5 by weight of said polyphosphate and said composition being capable of dissolving in water to give a dissolved polyphosphate concentration within the range of 0.1 grain per gallon to 5 grains per gallon of water and a dissolved nitrile concentration within the range of 0.05 grain per gallon to 0.5 grain per gallon of water.
- a method of inhibiting corrosion in water which is in contact with ferrous metals at temperatures above about 180 degrees F. which comprises essentially incorporating with the water so that both are present at the same time (1) a polyphosphate from the group consisting of sodium acid pyrophosphate, tetrasodium pyrophosphate, sodium tripolyphosphate, sodium tetraphosphate, calcium acid pyrophosphate, sodium trithiotetraphosphate, sodium hexametaphosphate and glassy septaphosphate and (2) a cyanide from the group consisting of sodium ferrocyanide, sodium nitroprusside, potassium ferrocyanide, sodium ferricyanide, potassium ferricyanide, sodium cyanide and stearyl nitrile, the quantity of said polyphosphate in said water being within the range of 0.1 grain per gallon to 5 grains per gallon of said water and the quantity of said cyanide in said water being within the range of 0.05 to 0.5 by weight of said polyphosphate.
- a polyphosphate from the group consisting
- a method of inhibiting corrosion in water which is in contact with ferrous metals at temperatures above about 180 degrees F. which comprises essentially incorporating with the water s0 peratures above about 180 degrees 1". which comprises essentially incorporating with the water so that both are present at the same time (1) a water soluble polyphosphate and (2) stearyl nitrile, the quantity of said polyphosphate in said water beingwithin the range of 0.1 grain per gallon to 5 grains per gallon of said water and the quantity o1 stearyl-nitrile in said water being within the range of 0.05 to 0.5 by weight of said polyphosphate.
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Preventing Corrosion Or Incrustation Of Metals (AREA)
Description
Patented July 18, 1950 CORROSION INHIBITIhiG COMPOSITIONS AND METHOD John W. Ryznar, La Grange Park, and Marjorie A. Peich, Chicago, IlL, assignors to National Aluminate Corporation, Chicago, 111., a corporation oi Delaware N Drawing. Application July 22, 1948, Serial No. 685,379
13 Claims. 1
This invention relates to new and improved corrosion inhibiting compositions'and to a new and improved method of inhibiting corrosion. The invention is particularly concerned with corrosion inhibiting compositions for preventing or inhibiting underwater corrosion in systems where water is moving, as through condensers, engine jackets, spray or cooling towers, and distribution systems. The invention is especially valuable in inhibitin corrosion of ferrous metals, including iron and steel.
It is known that various phosphates will inhibit underwater corrosion on ferrous metals under certain conditions. The dosage of the phosphate will vary depending upon such factors as the velocity of the water, the temperature and the chemical content of the water. Some phosphates are more efiective than others in certain types of waters. Thus, if the water contains very much calcium the use or an orthophosphate is undesirable because the calcium phosphate scale is deposited in the pipes and tubes, thereby producing a result which may be worse than the corrosion. The corroding tendency of the water is greatly increased by the presence of sodium chloride and sodium sulfate. As the velocity of the water increases the dosage of phosphate required to inhibit corrosion normally decreases, and as the temperature of the water is increased the dosage of phosphate to inhibit corrosion also increases.
n relatively corrosive waters at temperatures near the boiling point all corrosion cannot be stopped with phosphates alone, even when employing very high dosages of the phosphate. Our tests have indicated that with these very high dosages only partial protection can be obtained and there is localized corrosion which is very undesirable. The higher temperatures also produce a greater tendency toward scale formation where the water contains substantial amounts of calcium.
One of the objects of this invention is to provide new and improved corrosion inhibiting compositions.
A further object of the invention is to produce new and improved corrosion inhibiting compositions which are eilective in preventing or retarding the corrosive efiects of relatively corrosive waters on ferrous metals at relatively high temperatures.
Another object of the invention is to provide a new and improved method for inhibiting corrosion.
A still further object of the invention is to proi 2 vide a new and improved method of inhibiting corrosion by a chemical treatment involving the utilization of relati ely small amounts of corrosion inhibiting chemicals. Other objects will appear hereinafter.
In accordance with the invention new and improved corrosion inhibiting compositions are prepared by intimately mixing or blending a corrosion inhibiting phosphate with a compound containing a CN group, preferably a complex inorganic cyanide, with or without the addition of binders, algicides, bactericides and/or other water treating chemicals. Especially good results have been obtained with sodium ferrocyanide, sodium nitroprusside (NaaFe(CN) 5NO.2H20) potassium ferrocyanide, sodium ferricyanide and/or potassium ierricyanide in conjunction with a polyphosphate.
In order to evaluate the invention tests were made on a readily corrodible ferrous metal. namely, SAE-1020 mild steel, under various conditions of temperature and water velocity. The water used was a 1:1 mixture of Chicago tap water and distilled water, to which had been added 10.0 grains per gallon of sodium chloride. This water without treatment was very corrosive. When the water was treated with a polyphosphate such as sodium acid pyrophosphate (NazHaPrCr) or a molecularly dehydrated polyphosphate such as NaoP'iOaa, known as glassy septaphosphate. good protection against corrosion was obtained at degrees F. with relatively small amounts of the phosphate. At degrees F. relatively high dosages were required in order to inhibit corrosion. At degrees F. all corrosion could not be stopped even when very high dosages of phosphate were added. At this temperature and with these high dosages only partial protection could be obtained. This caused undesirable localized corrosion. The addition of a cyanide alone to the corrosive water could not inhibit corrosion. but the utilization of thephosphate in conjunction with a cyanide was effective in inhibiting the corrosion even at temperatures above 180 degrees F.
The invention will be further illustrated but is not limited by the following examples, in which the quantities are stated in parts by weight unless otherwise indicated.
MILE I A corrosive water was prepared as previously described by mixing Chicago tap water and distilled water in the ratio of 1:1 by weight and per gallon then adding 10.0 grains of sodium chlocorrosion protection at a temperature of 180 deride. This water was then used in various tests on SAE-1020 mild steel. The. tests were conducted by mounting a rod of BAE-l020 mild steel in a non-conducting mounting of Bakelite or rubber on a variable speed electric motor with the other end of the rod in the water to be tested. The velocity of the water can then be determined from the diameter of the rod and the speed at which the rod is turned by the motor. The water can be heated in any suitable manner to any desired temperature and maintained at that temperature. After each test the amount of corrosion can be determined by chemical analysis of the water for iron and by visual observation. Both methods'were used in evaluating the results hereinafter set forth.
The following table shows the dosage in grains per gallon of NSBHZP'I required for corrosion prevention of SAE-1020 'mild steel under various conditions of temperature and water velocity.
Indicates amount used was not s'uillcient to prevent all corrosion.
It will be observed that at 75 degrees F. good corrosion protection could be obtained with relatively small amounts of the hosphate. At 150 degrees F. quite high dosages were required but corrosion was inhibited by using the dosages shown. At 180 degrees F. and 210 degrees F. all corrosion could not be stopped even when very high dosages of the sodium acid pyrophosphate were employed except in one instance when the water velocity and dosage (15.0) were high. The use of such high dosages at these high temperatures is not only expensive but also causes other undesirable operating conditions such as sludge formation. Similar results were obtained with other phosphates, such as glassy septaphosphate. The use of cyanide compounds alone, such as sodium or potassium farm or ferricyanides, or sodium cyanide, did not substantially inhibit corrosion.
At a flow rate of 1.9 feet per second and 180 degrees F., using the same test conditions described under A, no corrosion was obtained when the water was treated with 1.0 grain per gallon of NaaP'zOm glassy septaphosphate and 0.1 grain per gallon of potassium ferrocyanide.
EXAMPLE II EXAMIPLEIII Tests made in the manner described under Example IA showed that 3.0 grains per gallon of NaoP'lOu glassy septaphosphate and 0.2 grain per gallon of sodium cyanide (NaCN) gave very good feet per second velocity.
EXAMPLE IV This example illustrates the preparation of a corrosion inhibiting composition suitable for the practice of the invention. Thi composition was prepared by pulverizing and blending together grees F. and 1.9
the following ingredients:
Ingredient: Parts by weight Sodium ferrocyanide 'I Glassy septaphosphate 50 Anhydrous tetrasodium pyrophosphate 28 Soda ash 15 The resultant pulverized composition can be added directly to the water to be treated.
EXAMPLE V A ball briquette was prepared by brlquetting the composition consisting of the following ingradients:
Anhydrous tetrasodium pyrophosphate 2'7 Ligno-sulfite binder (Bindarene) 8 Water 8 This composition can be used in a ball feeder for the treatment of water.
From the foregoing and many other tests it is apparent that the dosage of the cyanide need not be very high to exert a very marked effect in corrosion protection. The optimum amount of the cyanide is usually within the range of 0.05 to 0.5 of the phosphate, and very good results have been obtained when the amount of cyanide is around 0.33 of the amount of phosphate by weight. In terms of grains per gallon of water treated the ratio of phosphate is preferably within the range of 0.1 grain per gallon to 5 grains per gallon, and the ratio of cyanide is preferably within the range of 0.05 grain per gallon to 0.5 grain per gallon. Very excellent results have been obtained when only 0.1 grain per gallon of potassium ferrocyanide was added along with the phosphate.
The invention is not limited to the use of any a particular type of corrosion inhibiting phosphate.
If the temperature of the water treated is low and the calcium content is low orthophosphates can be used, as, for example, trisodium phosphate, monosodium dihydrogen phosphate and disodium monohydrogen phosphate. For overall purposes and at higher temperatures the use of a polyphosphate is preferred, including, for example, one or more of the following phosphates: sodium acid pyrophosphate, tetrasodium pyrophosphate, sodium tripolyphosphate (NaliPIiOlO), sodium tetraphosphate (Na4P6ol3), calcium acid pyrophosphate, sodium trithiotetraphosphate tially water insoluble, was also found to be eflective.
Throughout the specification and claims it will be understood that the expression "at a temperature near the boiling point" as applied to the water being treated is intended to include temperatures of at least about 180 degrees F.
In the tests which have been made to evaluate the invention neither the phosphates alone nor the cyanides alone were effective in. providing adequate corrosion protection at temperatures near the boiling point of water, whereas the combination of both was surprisingly effective. This improvement in the efiectiveness could not have been predicted 'from the existing knowledge of the chemistry and the behavior of these chemicals. The invention, therefore, provides new and useful water treating compositions which are effective in preventing corrosion over a wide range of temperature, and in waters that are normally very corrosive when not treated. The invention has important advantages in providing a method of protection against corrosion by the addition of relatively small amounts of substances which do not cause other undesirable operating conditions. The use of such relatively small amounts has the added advantage of reducing the cost of corrosion protection. Thus, it has been demonstrated in Example 13 that adequate corrosion protection at 180 degrees F. can be obtained with as little as 1.0 grain per gallon of glassy septaphosphate in conjunction with 0.1 grain per gallon of potassium ferricyanide, whereas, as shown by Table 1, without the addition of the cyanide, at the same water velocity the polyphosphate used did not give adequate corrosion protection when 6 grains per gallon were employed at 180 degrees F.
Having thus described the invention, what we claim is new and desire to secure by Letters Patent of the United States is:
1. A corrosion inhibiting composition comprising essentially a water soluble p lyphosphate and a water soluble inorganic complex cyanide, the ratio of said cyanide to said phosphate being within the range of 0.05 to 0.5 by weight of said phosphate, and said composition being capable of dissolving in water to give a dissolved phosphate concentration within the range of 0.1 grain per gallon to grains per gallon of water and a dissolved cyanide concentration within the range of 0.05 grain per gallon to 0.5 grain per gallon of water.
2. A corrosion inhibiting composition comprising essentially a water soluble glassy polyphosphate and a water soluble inorganic complex cyanide, the ratio of said cyanide to said phosphate being within the range 01 0.05 to 0.5 by weight of said phosphate, and said composition being capable of dissolving in water to give a dissolved phosphate concentration within the range of 0.1 grain per gallon to 5 grains per gallon of water and a dissolved cyanide concentration within the range of 0.05 grain per gallon to 0.5 grain per gallon of water.
3. A corrosion inhibiting composition comprising essentially a water soluble molecularly dehydrated phosphate and an alkali metal ferrocyanide, the ratio of said cyanide to said phosphate being within the range of 0.05 to 0.5 by weight oi said phosphate, and said composition being capable of dissolving in water to give a dissolved phosphate concentration within the range of 0.1 grain per gallon to 5 grains per gallon of water and a dissolved cyanide concentration within the range of 0.05 grain per gallon to 0.5 grain per gallon of water.
4. A corrosion inhibiting composition comprising essentially approximately 7% of sodium terrocyanide, approximately 50% of glassy septaphosphate, and approximately 27-28% of anhydrous tetrasodium pyrophosphate.
5. A method of inhibiting corrosion in water which is in contact with ferrous metals at temperatures above about degrees F. which comprises essentially incorporating with the water so that bpth are present at the same time (1) a polyphosphate and (2) a water soluble inorganic complex cyanide, the quantity of said polyphosphate in said water being within the range of 0.1 grain per gallon to 5 grains per gallon of said water, and the quantity of said inorganic cyanide in said water being within the range of 0.05 to 0.5 by weight of said polyphosphate.
6. A method of inhibiting corrosion in water which is in contact with ferrous metals at temperatures above about 180 degrees F. which comprises incorporating with the water so that both are present at the same time (1) a polyphosphate and (2) a water soluble potassium ferrocyanide, the quantity of said polyphosphate in said water being within the range of 0.1 grain per gallon to 5 grains per gallon of said water, and the quantity of said ferrocyanide in said water being within the range of 0.05 to 0.5 by weight of said polyphosphate.
7. A method of inhibiting corrosion in water at temperatures above about 180 degrees F. which comprises incorporating with the water so that both are present at the same time (1) a polyphosphate and (2) a water soluble potassium ferrocyanide, the quantity of polyphosphate being within the range of 1 to 5 grains per gallon, and the quantity of potassium ferrocyanide being within the range of 0.1 to 0.5 grains per gallon, the ratio of said ferrocyanide to said polyphosphate being within the range of 0.05 to 0.5 by weight of the polyphosphate.
8. A corrosion inhibiting composition comprising essentially a water soluble polyphosphate from the group consisting of sodium acid pyrophosphate, tetrasodium pyrophosphate, sodium tripolyphosphate, sodium tetraphosphate, calcium acid pyrophosphate, sodium trithiotetraphosphate, sodium hexametaphosphate and glassy septaphosphate, and a cyanide from the group consisting of sodium ferrocyanide, sodium nitroprusside, potassium ferrocyanide, sodium ferricyanide, potassium ferrlcyanide, sodium cyanide and stearyl nitrile, the ratio of said cyanide to said polyphosphate being within the range of 0.05 to 0.5 by weight of said polyphosphate and said composition being capable of dissolving in water to give a dissolved polyphosphate concentration within the range of 0.1 grain per gallon to 5 grains per gallon of water and a dissolved cyanide concentration within. the range of 0.05 grain per gallon to 0.5 grain per gallon of water.
9. A corrosion inhibiting composition comprising essentially a water soluble polyphosphate and sodium cyanide, the ratio of said cyanide to said polyphosphate being Within the range of 0.05 to 0.5 by weight of said polyphosphate and said composition being capable of dissolving in water to give a dissolved polyphosphate concentration within the range of 0.1 grain per gallon to 5 grains per gallon of water and a dissolved cyanide concentration within the range of 0.05 grain per gallon to 0.5 grain per gallon of water.
10. A corrosion inhibiting composition comprising essentially a water soluble polyphosphate and stearyl nitrile, the ratio of said nitrile to said polyphosphate being within the range of 0.05 to 0.5 by weight of said polyphosphate and said composition being capable of dissolving in water to give a dissolved polyphosphate concentration within the range of 0.1 grain per gallon to 5 grains per gallon of water and a dissolved nitrile concentration within the range of 0.05 grain per gallon to 0.5 grain per gallon of water.
11. A method of inhibiting corrosion in water which is in contact with ferrous metals at temperatures above about 180 degrees F. which comprises essentially incorporating with the water so that both are present at the same time (1) a polyphosphate from the group consisting of sodium acid pyrophosphate, tetrasodium pyrophosphate, sodium tripolyphosphate, sodium tetraphosphate, calcium acid pyrophosphate, sodium trithiotetraphosphate, sodium hexametaphosphate and glassy septaphosphate and (2) a cyanide from the group consisting of sodium ferrocyanide, sodium nitroprusside, potassium ferrocyanide, sodium ferricyanide, potassium ferricyanide, sodium cyanide and stearyl nitrile, the quantity of said polyphosphate in said water being within the range of 0.1 grain per gallon to 5 grains per gallon of said water and the quantity of said cyanide in said water being within the range of 0.05 to 0.5 by weight of said polyphosphate.
12, A method of inhibiting corrosion in water which is in contact with ferrous metals at temperatures above about 180 degrees F. which comprises essentially incorporating with the water s0 peratures above about 180 degrees 1". which comprises essentially incorporating with the water so that both are present at the same time (1) a water soluble polyphosphate and (2) stearyl nitrile, the quantity of said polyphosphate in said water beingwithin the range of 0.1 grain per gallon to 5 grains per gallon of said water and the quantity o1 stearyl-nitrile in said water being within the range of 0.05 to 0.5 by weight of said polyphosphate.
JOHN W. RYZNAR.
MARJORIE A. PEICH.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PA'IENTB Number Name Date 1,926,265 Darsey Sept. 12, 1933 1,942,923 Irion Jan. 9, 1934 2,120,212 Curtin June 7, 1938 2,332,209 Enquist Oct. 19, 1943 2,337,856 Rice et a1 Dec. 28, 1943
Claims (1)
1. A CORROSION INHIBITING COMPOSITION COMPRISING ESSENTIALLY A WATER SOLUBLE POLYPHOSPHATE AND A WATER SOLUBLE INORGANIC COMPLEX CYANIDE, THE RATIO OF SAID CYANIDE TO SAID PHOSPHATE BEING WITHIN THE RANGE OF 0.05 TO 0.5 BY WEIGHT OF SAID PHOSPHATE, AND SAID COMPOSITION BEING CAPABLE OF DISSOLVING IN WATER TO GIVE A DISSOLVED PHOSPHATE CONCENTRATION WITHIN THE RANGE OF 0.1 GRAIN PER GALLON TO 5 GRAINS PER GALLON OF WATER AND A DISSOLVED CYANIDE CONCENTRATION WITHIN THE RANGE OF 0.05 PER GALLON TO 0.5 GRAIN PER GALLON OF WATER.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US685379A US2515529A (en) | 1946-07-22 | 1946-07-22 | Corrosion inhibiting compositions and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US685379A US2515529A (en) | 1946-07-22 | 1946-07-22 | Corrosion inhibiting compositions and method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2515529A true US2515529A (en) | 1950-07-18 |
Family
ID=24751955
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US685379A Expired - Lifetime US2515529A (en) | 1946-07-22 | 1946-07-22 | Corrosion inhibiting compositions and method |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2515529A (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2748035A (en) * | 1953-07-21 | 1956-05-29 | Detrex Corp | Method of and composition for cleaning containers containing aluminum and tin |
| US3018167A (en) * | 1957-10-17 | 1962-01-23 | Monsanto Chemicals | Method for producing trimetaphosphimic acid |
| US3019195A (en) * | 1959-05-01 | 1962-01-30 | Dearborn Chemicals Co | Method and composition for treating cooling water |
| US3039844A (en) * | 1957-10-17 | 1962-06-19 | Monsanto Chemicals | O-tolidine salt of trimetaphosphimic acid corrosion inhibitor |
| US3723162A (en) * | 1969-12-30 | 1973-03-27 | Bayer Ag | Pretreatment of metal surfaces |
| US3887488A (en) * | 1972-03-08 | 1975-06-03 | Celanese Corp | Inhibition of corrosion in sulfuric acid solutions |
| US3960735A (en) * | 1974-08-15 | 1976-06-01 | Early California Industries, Inc. | Corrosion-inhibited polyphosphate compositions |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1926265A (en) * | 1930-12-08 | 1933-09-12 | Metal Finishing Res Corp | Coating metal with zinc phosphate |
| US1942923A (en) * | 1932-11-11 | 1934-01-09 | Battelle Memorial Institute | Method of treating copper and copper alloys |
| US2120212A (en) * | 1936-01-10 | 1938-06-07 | Curtin Howe Corp | Phosphated metal coating |
| US2332209A (en) * | 1941-08-11 | 1943-10-19 | Melvin A Enquist | Water treating method |
| US2337856A (en) * | 1942-10-27 | 1943-12-28 | Hall Lab Inc | Process of retarding the corrosion of metal by water |
-
1946
- 1946-07-22 US US685379A patent/US2515529A/en not_active Expired - Lifetime
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1926265A (en) * | 1930-12-08 | 1933-09-12 | Metal Finishing Res Corp | Coating metal with zinc phosphate |
| US1942923A (en) * | 1932-11-11 | 1934-01-09 | Battelle Memorial Institute | Method of treating copper and copper alloys |
| US2120212A (en) * | 1936-01-10 | 1938-06-07 | Curtin Howe Corp | Phosphated metal coating |
| US2332209A (en) * | 1941-08-11 | 1943-10-19 | Melvin A Enquist | Water treating method |
| US2337856A (en) * | 1942-10-27 | 1943-12-28 | Hall Lab Inc | Process of retarding the corrosion of metal by water |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2748035A (en) * | 1953-07-21 | 1956-05-29 | Detrex Corp | Method of and composition for cleaning containers containing aluminum and tin |
| US3018167A (en) * | 1957-10-17 | 1962-01-23 | Monsanto Chemicals | Method for producing trimetaphosphimic acid |
| US3039844A (en) * | 1957-10-17 | 1962-06-19 | Monsanto Chemicals | O-tolidine salt of trimetaphosphimic acid corrosion inhibitor |
| US3019195A (en) * | 1959-05-01 | 1962-01-30 | Dearborn Chemicals Co | Method and composition for treating cooling water |
| US3723162A (en) * | 1969-12-30 | 1973-03-27 | Bayer Ag | Pretreatment of metal surfaces |
| US3887488A (en) * | 1972-03-08 | 1975-06-03 | Celanese Corp | Inhibition of corrosion in sulfuric acid solutions |
| US3960735A (en) * | 1974-08-15 | 1976-06-01 | Early California Industries, Inc. | Corrosion-inhibited polyphosphate compositions |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4406811A (en) | Composition and method for controlling corrosion in aqueous systems | |
| US3959167A (en) | Method and composition of inhibiting scale | |
| US3738806A (en) | Process for the prevention of corrosion | |
| CA1113238A (en) | Anti-corrosion composition | |
| US3099521A (en) | Water treatment | |
| US2515529A (en) | Corrosion inhibiting compositions and method | |
| US3699047A (en) | Coolant system and corrosion inhibitor and method of use | |
| USRE23740E (en) | Corrosion inhibiting compositions | |
| CN103864232B (en) | General corrosion and scale inhibitor for purifying circulating water and preparation and application thereof | |
| US4717542A (en) | Inhibiting corrosion of iron base metals | |
| US4666609A (en) | Water treatment agent | |
| US4529572A (en) | Polymer-zinc corrosion inhibitor | |
| US3714067A (en) | Methods of inhibiting corrosion with condensed polyalkylenepolyamine phosphonates | |
| US3718603A (en) | Methods of inhibiting corrosion with substituted tertiary amine phosphonates | |
| US2855286A (en) | Process and composition for reducing corrosion of metals | |
| US2901437A (en) | Corrosion inhibiting composition | |
| CN105036365A (en) | Draught fan dedusting stripping scale inhibitor and preparation method thereof | |
| JPS5937750B2 (en) | metal corrosion inhibitor | |
| US3036305A (en) | Treatment of water | |
| US2890928A (en) | Corrosion inhibition | |
| US4168230A (en) | Synergistic composition comprising phosphorylated ethoxylated glycerine and polyacrylic acid for the prevention of CaCO3 scale in cooling water | |
| US3476689A (en) | Composition for use in stabilizing calcium carbonate in cooling water | |
| US3019195A (en) | Method and composition for treating cooling water | |
| CN106430652B (en) | A kind of corrosion inhibiter and composite slow-corrosion scale resistor and their application | |
| CA1289293C (en) | Polymer-zinc corrosion inhibitor |