US3754990A - Cleaning of ferrous metal surfaces - Google Patents
Cleaning of ferrous metal surfaces Download PDFInfo
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- US3754990A US3754990A US00117806A US3754990DA US3754990A US 3754990 A US3754990 A US 3754990A US 00117806 A US00117806 A US 00117806A US 3754990D A US3754990D A US 3754990DA US 3754990 A US3754990 A US 3754990A
- Authority
- US
- United States
- Prior art keywords
- solution
- copper
- cleaning
- ferrous metal
- cleaning solution
- 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
- 238000004140 cleaning Methods 0.000 title claims abstract description 45
- 239000002184 metal Substances 0.000 title claims abstract description 29
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 29
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 title claims abstract description 22
- 239000000243 solution Substances 0.000 claims abstract description 48
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims abstract description 34
- 229910052802 copper Inorganic materials 0.000 claims abstract description 33
- 239000010949 copper Substances 0.000 claims abstract description 33
- 230000006872 improvement Effects 0.000 claims description 10
- 239000007864 aqueous solution Substances 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 5
- 239000012535 impurity Substances 0.000 claims description 2
- 239000002253 acid Substances 0.000 abstract description 19
- 229920000768 polyamine Polymers 0.000 abstract description 19
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 abstract description 16
- 239000002738 chelating agent Substances 0.000 abstract description 13
- 235000013980 iron oxide Nutrition 0.000 abstract description 11
- VBMVTYDPPZVILR-UHFFFAOYSA-N iron(2+);oxygen(2-) Chemical class [O-2].[Fe+2] VBMVTYDPPZVILR-UHFFFAOYSA-N 0.000 abstract description 7
- 239000012670 alkaline solution Substances 0.000 abstract description 5
- 239000002244 precipitate Substances 0.000 abstract description 5
- 125000003277 amino group Chemical group 0.000 abstract description 4
- 238000000034 method Methods 0.000 description 21
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 15
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 description 12
- 229920002873 Polyethylenimine Polymers 0.000 description 9
- 230000008569 process Effects 0.000 description 8
- 229910021529 ammonia Inorganic materials 0.000 description 7
- 150000001412 amines Chemical class 0.000 description 6
- 239000000203 mixture Substances 0.000 description 6
- 238000005260 corrosion Methods 0.000 description 5
- 230000007797 corrosion Effects 0.000 description 5
- 239000003112 inhibitor Substances 0.000 description 5
- NOWKCMXCCJGMRR-UHFFFAOYSA-N Aziridine Chemical compound C1CN1 NOWKCMXCCJGMRR-UHFFFAOYSA-N 0.000 description 4
- 150000007513 acids Chemical class 0.000 description 4
- 125000004432 carbon atom Chemical group C* 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000007795 chemical reaction product Substances 0.000 description 4
- -1 ferrous metals Chemical class 0.000 description 4
- 239000011521 glass Substances 0.000 description 4
- 239000000758 substrate Substances 0.000 description 4
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 3
- 238000000151 deposition Methods 0.000 description 3
- VLDHWMAJBNWALQ-UHFFFAOYSA-M sodium;1,3-benzothiazol-3-ide-2-thione Chemical compound [Na+].C1=CC=C2SC([S-])=NC2=C1 VLDHWMAJBNWALQ-UHFFFAOYSA-M 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- XKWFRVVFRZYIFP-UHFFFAOYSA-N triazanium;2-[2-[bis(carboxylatomethyl)amino]ethyl-(carboxymethyl)amino]acetate Chemical compound N.N.N.OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O XKWFRVVFRZYIFP-UHFFFAOYSA-N 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical compound ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 2
- YKNKBBMRKMLLJS-UHFFFAOYSA-N 1-phenylaziridine Chemical compound C1CN1C1=CC=CC=C1 YKNKBBMRKMLLJS-UHFFFAOYSA-N 0.000 description 2
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 2
- KWOLFJPFCHCOCG-UHFFFAOYSA-N Acetophenone Chemical compound CC(=O)C1=CC=CC=C1 KWOLFJPFCHCOCG-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical group C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 2
- QUSNBJAOOMFDIB-UHFFFAOYSA-N Ethylamine Chemical compound CCN QUSNBJAOOMFDIB-UHFFFAOYSA-N 0.000 description 2
- 239000005977 Ethylene Substances 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 239000003929 acidic solution Substances 0.000 description 2
- 230000004913 activation Effects 0.000 description 2
- 125000002947 alkylene group Chemical group 0.000 description 2
- 125000002057 carboxymethyl group Chemical group [H]OC(=O)C([H])([H])[*] 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 235000014113 dietary fatty acids Nutrition 0.000 description 2
- 229930195729 fatty acid Natural products 0.000 description 2
- 239000000194 fatty acid Substances 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 125000000896 monocarboxylic acid group Chemical group 0.000 description 2
- LSHROXHEILXKHM-UHFFFAOYSA-N n'-[2-[2-[2-(2-aminoethylamino)ethylamino]ethylamino]ethyl]ethane-1,2-diamine Chemical compound NCCNCCNCCNCCNCCN LSHROXHEILXKHM-UHFFFAOYSA-N 0.000 description 2
- 125000004433 nitrogen atom Chemical group N* 0.000 description 2
- 238000007747 plating Methods 0.000 description 2
- 229920001281 polyalkylene Polymers 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 238000006467 substitution reaction Methods 0.000 description 2
- GETQZCLCWQTVFV-UHFFFAOYSA-N trimethylamine Chemical compound CN(C)C GETQZCLCWQTVFV-UHFFFAOYSA-N 0.000 description 2
- CBQCUNYUJWJFTB-UHFFFAOYSA-N 2-(2,2-diaminoethylsulfanyl)ethane-1,1-diamine Chemical compound NC(N)CSCC(N)N CBQCUNYUJWJFTB-UHFFFAOYSA-N 0.000 description 1
- URDCARMUOSMFFI-UHFFFAOYSA-N 2-[2-[bis(carboxymethyl)amino]ethyl-(2-hydroxyethyl)amino]acetic acid Chemical compound OCCN(CC(O)=O)CCN(CC(O)=O)CC(O)=O URDCARMUOSMFFI-UHFFFAOYSA-N 0.000 description 1
- 229910001018 Cast iron Inorganic materials 0.000 description 1
- QPLDLSVMHZLSFG-UHFFFAOYSA-N Copper oxide Chemical compound [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 description 1
- 239000005751 Copper oxide Substances 0.000 description 1
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 1
- RPNUMPOLZDHAAY-UHFFFAOYSA-N Diethylenetriamine Chemical compound NCCNCCN RPNUMPOLZDHAAY-UHFFFAOYSA-N 0.000 description 1
- ROSDSFDQCJNGOL-UHFFFAOYSA-N Dimethylamine Chemical compound CNC ROSDSFDQCJNGOL-UHFFFAOYSA-N 0.000 description 1
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 1
- 229910001209 Low-carbon steel Inorganic materials 0.000 description 1
- QPCDCPDFJACHGM-UHFFFAOYSA-N N,N-bis{2-[bis(carboxymethyl)amino]ethyl}glycine Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(=O)O)CCN(CC(O)=O)CC(O)=O QPCDCPDFJACHGM-UHFFFAOYSA-N 0.000 description 1
- JYXGIOKAKDAARW-UHFFFAOYSA-N N-(2-hydroxyethyl)iminodiacetic acid Chemical compound OCCN(CC(O)=O)CC(O)=O JYXGIOKAKDAARW-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- IGFHQQFPSIBGKE-UHFFFAOYSA-N Nonylphenol Natural products CCCCCCCCCC1=CC=C(O)C=C1 IGFHQQFPSIBGKE-UHFFFAOYSA-N 0.000 description 1
- 229930040373 Paraformaldehyde Natural products 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 125000003172 aldehyde group Chemical group 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 150000003934 aromatic aldehydes Chemical class 0.000 description 1
- 229910000963 austenitic stainless steel Inorganic materials 0.000 description 1
- ZVDNYZRDGKYYAE-UHFFFAOYSA-N azane 2-[carboxymethyl(2-hydroxyethyl)amino]acetic acid Chemical compound OCCN(CC(=O)O)CC(=O)O.N ZVDNYZRDGKYYAE-UHFFFAOYSA-N 0.000 description 1
- FDIWRLNJDKKDHB-UHFFFAOYSA-N azanium;2-aminoacetate Chemical compound [NH4+].NCC([O-])=O FDIWRLNJDKKDHB-UHFFFAOYSA-N 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 150000001555 benzenes Chemical class 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 229910001431 copper ion Inorganic materials 0.000 description 1
- 229910000431 copper oxide Inorganic materials 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 230000002452 interceptive effect Effects 0.000 description 1
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- MGFYIUFZLHCRTH-UHFFFAOYSA-N nitrilotriacetic acid Chemical compound OC(=O)CN(CC(O)=O)CC(O)=O MGFYIUFZLHCRTH-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- SNQQPOLDUKLAAF-UHFFFAOYSA-N nonylphenol Chemical compound CCCCCCCCCC1=CC=CC=C1O SNQQPOLDUKLAAF-UHFFFAOYSA-N 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- NDLPOXTZKUMGOV-UHFFFAOYSA-N oxo(oxoferriooxy)iron hydrate Chemical compound O.O=[Fe]O[Fe]=O NDLPOXTZKUMGOV-UHFFFAOYSA-N 0.000 description 1
- 229920002866 paraformaldehyde Polymers 0.000 description 1
- 229960003330 pentetic acid Drugs 0.000 description 1
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000003784 tall oil Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
- C11D3/16—Organic compounds
- C11D3/26—Organic compounds containing nitrogen
- C11D3/33—Amino carboxylic acids
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D3/00—Other compounding ingredients of detergent compositions covered in group C11D1/00
- C11D3/16—Organic compounds
- C11D3/37—Polymers
- C11D3/3703—Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- C11D3/3723—Polyamines or polyalkyleneimines
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D7/00—Compositions of detergents based essentially on non-surface-active compounds
- C11D7/22—Organic compounds
- C11D7/32—Organic compounds containing nitrogen
- C11D7/3209—Amines or imines with one to four nitrogen atoms; Quaternized amines
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D7/00—Compositions of detergents based essentially on non-surface-active compounds
- C11D7/22—Organic compounds
- C11D7/32—Organic compounds containing nitrogen
- C11D7/3245—Aminoacids
-
- 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
- C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
- C23G1/00—Cleaning or pickling metallic material with solutions or molten salts
- C23G1/14—Cleaning or pickling metallic material with solutions or molten salts with alkaline solutions
- C23G1/19—Iron or steel
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D2111/00—Cleaning compositions characterised by the objects to be cleaned; Cleaning compositions characterised by non-standard cleaning or washing processes
- C11D2111/10—Objects to be cleaned
- C11D2111/14—Hard surfaces
- C11D2111/16—Metals
Definitions
- ABSTRACT Richman Attorney-Griswold & Burdick [5 7] ABSTRACT
- the invention is based on the discovery that upon adding a polyamine having intralinear amino groups to an aqueous alkaline solution of an ammoniated or aminated polycarboxylic acid chelating agent, a new and improved metal cleaning solution is provided. Upon bringing such cleaning solution into contact with a ferrous metal surface having hardness and/or iron oxide scale, and copper, thereon and the solution being maintained at a temperature above about 155C. for a time sufficient to dissolve all the hardness and iron oxides, the copper is dissolved and neither precipitates from solution nor deposits on the ferrous metal surface.
- the invention relates to an improvement in the method of cleaning ferrous metal surfaces, such as steam boilers having copper components in the system, with an aqueous alkaline solution of polycarboxylic acid chelating agent and to the aqueous cleaning composition employed in the improved process.
- the cleaning solutions consist of an ammoniated or aminated polycarboxylic acid chelating agent and cleaning is carried out under alkaline conditions.
- This method is effective for the removal of mill-scale and hardness deposits, but is not very effective for the removal of mill-scale having copper deposits thereon.
- aqueous cleaning solutions containing a polycarboxylic acid chelating agent may be modified in an attempt to make the solutions suitable for working with copper deposits.
- a reagent may be added to the cleaning solution which will form a precipitate with the copper removed in cleaning and prevent its deposition on freshly cleaned ferrous metal surfaces.
- Such a process suffers from the disadvantage that care must be taken to dislodge and remove all of the copper precipitate, usually by a rinse involving a considerable volume of water.
- a principal object of the present invention is to provide an improvement in the method of cleaning a ferrous metal surface, having iron oxides and copper deposited thereon, using an ammoniated or aminated polycarboxylic acid chelating agent, the improvement providing for removal of iron oxides and copper in one operation while avoiding deposition of copper on the freshly cleaned metal substrate.
- the invention is based on the discovery that upon adding a polyamine having intralinear amino groups to an aqueous alkaline solution of an ammoniated or aminated polycarboxylic acid chelating agent, a new and improved metal cleaning solution is provided. Upon bringing such cleaning solution into contact with a ferrous metal surface having hardness and/or iron oxide scale, and copper, thereon and the solution being maintained at a temperature above about C. for a time sufficient to dissolve all the hardness and iron oxides, the copper is dissolved and neither precipitates from solution nor deposits on the ferrous metal surface.
- ferrous metal surfaces may be cleaned using the solution and method of the invention.
- ferrous metals are cast iron, mild steel, and austenitic stainless steel.
- Suitable polycarboxylic acid chelating agents include the alkylene polyamine polyacetic acids of the formula (HOOCCH,) N[(CH,),,N(CI-I COOH)],,,CI-I COOH wherein n is 1,2,3 or 4 and m is 0,l,2,3, or 4, up to two of the carboxymethyl groups may be replaced with a B-hydroxyethyl group and one or more of the carboxymethyl groups may be replaced by carboxyethyl groups.
- polyacetic acids which are particularly suitable are ethylenediaminetetraacetic acid (EDTA), N-hydroxyethyl ethylenediaminetriacetic acid, nitrilotriacetic acid, N-2-hydroxyethyliminodiacetic acid, diethylenetriamine-pentaacetic acid, and mixtures thereof.
- EDTA ethylenediaminetetraacetic acid
- N-hydroxyethyl ethylenediaminetriacetic acid N-hydroxyethyl ethylenediaminetriacetic acid
- nitrilotriacetic acid nitrilotriacetic acid
- N-2-hydroxyethyliminodiacetic acid diethylenetriamine-pentaacetic acid
- Such polycarboxylic acid chelating agents must be combined with ammonia or a suitable amine in order to obtain a solution with a basic pH. Solution pH can be further adjusted by the use of additional ammonia or amine.
- Amine Pol carboxylic Acid ammonia EDTA ethanolamine EDTA ethylamine EDTA ethylenediamine EDTA diethylenetriamine EDTA pentaethylenehexamine EDTA dirnethylamine EDTA trimethylamine EDTA ethylenimine EDTA ethanolamine ethylenediaminetetrapropionic acid ethylenediamine N,N-di (fl-hydroxyethyl) glycine ammonia tetramethylenediamine- N,N,N',N'-tetraacetic acid ammonia (2-hydroxyethylimino) diacetic acid Any of the combinations of polycarboxylic acids and ammonia or amines considered together may be used in a concentration in the range of about 1 to 10 per cent by weight.
- the polyamines which may be used are principally the polyalkylene polyamines having intralinear amino groups having a ratio of nitrogen atoms to carbon atoms in the chain of at least about 0.2 and preferably at least about 0.5.
- suitable polyamines must be readily soluble in the aqueous cleaning solution at an alkaline pH in the range of pH 7 to 10.
- Specific examples of suitable polyamines are polyethylenimine having molecular weights in the range of about 600 to 500,000, the reaction product of ethylenediamine and ethylenedichloride having an average molecular weight above about 230, preferably about 600 to 500,000, copolymerized N-phenyl ethylenimine and ethylenimine,
- the copolymer having an n-phenyl group on about 10 per cent of the ethylene units in the molecule, and pentaethylenehexamine.
- the polyamines are employed in a concentration range of about 0.2 to per cent by weight. In any event, a sufficient amount of the polyamine must be used to provide two nitrogen atoms for each copper ion which is to be complexed. The amount of polyethylenimine to meet this requirement is about 2.8 parts per part by weight of copper.
- the corrosive attack of the polycarboxylic acid chelating agent upon the metal substrate is inhibited by an inhibitor compound or composition that does not interfere with the action of the present polyamines in keeping copper from plating out on the substrate.
- suitable inhibitors include, e.g.
- the system in carrying out the improved process as on a boiler system, the system is drained and then refilled with an aqueous alkaline solution of the polycarboxylic acid chelating agent having the polyamine dissolved therein.
- the aqueous solution is heated up in order to dissolve iron oxide or hardness deposits at practical rates.
- the solution is also heated in order to activate the polyamine.
- temperatures above about 155C are employed. Suitable temperatures are in the range of 155 to 190C.
- the cleaning solution builds up some autogenous pressure due to the water and the ammonia or other volatile amine present. Pressure of the order of 20 to 200 pounds per square inch gauge are typical, but have no particular effect on the present method.
- the temperature of the cleaning solution is maintained for at least 30 to 60 minutes, or until the iron oxides and other deposits are removed. The process seldom takes more than 4 hours. At the end of this time the cleaning solution is drained and rinsed leaving a clean ferrous metal surface free of copper deposits.
- the polyamine is activated by heating an aqueous solution thereof prior to adding the polyamine to the aqueous alkaline cleaing solution containing the polycarboxylic acid chelating agent. Heating about 10 per cent by weight aqueous solution of the polyamine to a temperature of at least 155C. and preferably 160 to 190C. for 30 minutes provides sufficient pyrolytic activation of the polyamine. With such prior activation outside the system to be cleaned, the cleaning of the ferrous metal surface may proceed at a much lower temperature, usually in the range of 110 to 150C. The advantage of using such lower temperature is decreased corrosion of the ferrous metal surface by the cleaning solution, without in any way interfering with the removal of copper deposits.
- EXAMPLE I An aqueous solution was prepared containing 3.8 per cent by weight of triammonium (ethylenedinitrilo) tetraacetate (ammoniated EDTA), 0.3 per cent by weight of polyethylenimine having a molecular weight of about 40,000 to 60,000, 0.05 per cent by weight of sodium mercaptobenzothiazole and 0.1 per cent by weight of a commercial inhibitor of the class described in U.S. Pat. No. 3,077,454 and consisting of the product of reaction of Rosin Amine D, tall oil fatty acids, acetophenone, and paraformaldehyde at a temperature of about C. for about 8 hours in ethylene glycol medium and in the presence of H 80 After the reaction, an adduct of nonylphenol and ethylene oxide was added to the reaction product all as more fully described in said U.S. patent.
- a 200 milliliter quantity of this solution was placed in a glass beaker along with two 1010 (AISI) steel coupons having a natural mill-scale surface thereon.
- AISI 1010
- 0.3 grams of copper powder admixed with 0.7 grams of ferric oxide powder were also placed in the same glass beaker.
- the beaker and contents were placed in a pressure vessel. The vessel was closed and heated to 187C. The autogenous pressure in the vessel rose to pounds per square inch gauge. After 4 hours at the stated temperature the reactor was quenched with water and opened. The beaker and contents were removed.
- the coupons were found to be bright and clear and free of copper deposits.
- EXAMPLE 2 On carrying out a run in the same manner as Example 1 except that a polyethylenimine having 10 per cent phenyl substitution in the molecule was substituted weight-by-weight for the polyethylenimine of example 1, the mill-scale coated coupons were cleaned and copper did not deposit on the cleaned surfaces.
- COMPARlSON TEST In a run made by way of comparison, all conditions and reactants were the same as in example 1 except that the pressure vessel and contents were heated only to 119C. The coupons were cleaned of mill-scale but carried heavy copper deposit.
- EXAMPLE 4 A solution containing 3.8 per cent by weight of triammonium (ethylenedinitrilo)tetraacetate, and 0.25 per cent by weight of a polyethylenimine having a molecular weight of approximately 50,000 was prepared and 200 milliliters of this solution was placed in a glass beaker along with two 1010(AIS1) steel coupons which had been cleaned in nitric acid, dried and weighed. The beaker and contents were placed in a pressure vessel and heated to 150C. The temperature was maintained for 4 hours after which the pressure vessel was quenched and opened. The coupons were dried and weighed and corrosion of the metal was found to have taken place at the rate of 0.0605 pounds per square foot per day (lb/ftF/day).
- EXAMPLE 6 A run was carried out in the same manner as example 5 except that sodium mercaptobenzothiazole and the commercial inhibitor described in example 1 were added to the last solution in the same proportions as in Example 1. The coupons subject to test corroded at a rate of 0.0043 lb/ftF/day.
- EXAMPLE 7 A solution containing 3.8 per cent by weight of triammonium (ethylenedinitrilo)tetraacetate and 0.3 per cent by weight polyethylenimine and 0.15 per cent by weight copper oxide was prepared and 200 milliliters of this solution was placed in a glass beaker. The beaker was placed in a pressure vessel and the vessel and contents were heated to 160C for about 30 minutes. The pressure vessel was then cooled and opened and two 1010(AIS1) steel coupons having a surface covered with mill-scale were placed in the beaker. The pressure vessel was then closed and heated to l C. The temperature was maintained for 4 hours, after which the pressure vessel was cooled and opened and the coupons examined. The coupons were found to be free of copper plating and they showed corrosion had taken place at the rate of 0.0173 lb/ftlday.
- the polyalkylenepolyamine having an average molecular weight in the range of about 40,000 to 60,000 and being selected from the group consisting of polymerized ethylenimine, the reaction product of ethylenediamine and ethylenedichloride, and copolymerized N-phenyl ethylenimine and ethylenimine having an N-phenyl group on about 10 per cent of the ethylene units in the molecule.
- aqueous cleaning solution is initially heated to a temperature in the range of above about 155 and up to 190C, and then the temperature is reduced to about 1 10 to C for the balance of the cleaning period.
- the cleaning solution contains from 0.1 to 5 per cent by weight of polyalkylenepolyamine
- the cleaning solution is activated by heating to a temperature in the range of above about and up to C and thereafter the cleaning solution is maintained in contact with the ferrous metal surface at a temperature in the range of 1 10 to 150C.
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Abstract
The invention is based on the discovery that upon adding a polyamine having intralinear amino groups to an aqueous alkaline solution of an ammoniated or aminated polycarboxylic acid chelating agent, a new and improved metal cleaning solution is provided. Upon bringing such cleaning solution into contact with a ferrous metal surface having hardness and/or iron oxide scale, and copper, thereon and the solution being maintained at a temperature above about 155*C. for a time sufficient to dissolve all the hardness and iron oxides, the copper is dissolved and neither precipitates from solution nor deposits on the ferrous metal surface.
Description
United States Patent [1 1 Teumac et a1.
[451 Aug. 23, 1973 1 CLEANING OF FERROUS METAL SURFACES [75] inventors: Fred Norman Teumac, Charlotte,
N.C.; James Scott Scruggs, Lake Jackson, Tex.
Related 1.1.8. Application Data [62] Division of Ser. No. 704,265, Feb. 9, 1968, Pat. No.
[52] US. Cl 134/2, 134/3, 134/22 R, 252/82, 252/156, 252/546, 252/DIG. ll
[51] Int. Cl C23g l/18, C23g l/26, 1308b 9/08 [58] Field of Search 252/D1G. 11, 546, 252/156, 82; 134/2, 3, 22 R, 41
3,251,778 5/1966 Dickson et a1 252/82 3,262,791 7/1966 Dickson et al 252/390 X 3,308,065 3/1967 Lesinski 252/546 X 3,438,901 4/1969 Vassileff.... 252/82 UX 3,440,170 4/1969 de Hek 134/3 X 3,447,965 6/1969 Teumac 134/3 X 3,490,741 l/l970 Teumac et a1. 134/3 X FOREIGN PATENTS OR APPLlCATlONS 821,094 9/1959 Great Britain 134/22 R Primary Examiner-Barry S. Richman Attorney-Griswold & Burdick [5 7] ABSTRACT The invention is based on the discovery that upon adding a polyamine having intralinear amino groups to an aqueous alkaline solution of an ammoniated or aminated polycarboxylic acid chelating agent, a new and improved metal cleaning solution is provided. Upon bringing such cleaning solution into contact with a ferrous metal surface having hardness and/or iron oxide scale, and copper, thereon and the solution being maintained at a temperature above about 155C. for a time sufficient to dissolve all the hardness and iron oxides, the copper is dissolved and neither precipitates from solution nor deposits on the ferrous metal surface.
4 Claims, No Drawings CLEANING OF FERROUS METAL SURFACES CROSS-REFERENCE TO RELATED APPLICATION This is a division of application Ser. No. 704,265, filed Feb. 9, 1968 and now US. Pat. No. 3,627,687.
BACKGROUND OF THE INVENTION 1. Field of the Invention The invention relates to an improvement in the method of cleaning ferrous metal surfaces, such as steam boilers having copper components in the system, with an aqueous alkaline solution of polycarboxylic acid chelating agent and to the aqueous cleaning composition employed in the improved process.
2. Description of the Prior Art A process for cleaning ferrous metal surfaces has been used in which iron oxides are first removed in an initial cleaning step using an aqueous acidic solution of a polycarboxylic acid, after which the solution is made alkaline and a copper removal step is effectedv However, it is generally considered better practice to avoid using acidic solutions for the cleaning of boiler systems. Further, two-step methods are not as economical, generally, as one-step methods.
In another process disclosed in U.S. Pat. No. 3,308,065, the cleaning solutions consist of an ammoniated or aminated polycarboxylic acid chelating agent and cleaning is carried out under alkaline conditions. This method is effective for the removal of mill-scale and hardness deposits, but is not very effective for the removal of mill-scale having copper deposits thereon.
Several methods may be used to modify aqueous cleaning solutions containing a polycarboxylic acid chelating agent in an attempt to make the solutions suitable for working with copper deposits. For example, a reagent may be added to the cleaning solution which will form a precipitate with the copper removed in cleaning and prevent its deposition on freshly cleaned ferrous metal surfaces. Such a process suffers from the disadvantage that care must be taken to dislodge and remove all of the copper precipitate, usually by a rinse involving a considerable volume of water.
It has also been suggested to add an oxidizing agent to the cleaning solution subsequent to removal of the mill-scale in order to dissolve the copper plated on the clean substrate. This method also suffers from the disadvantage that it is a two-step process.
OBJECTS OF THE INVENTION A principal object of the present invention is to provide an improvement in the method of cleaning a ferrous metal surface, having iron oxides and copper deposited thereon, using an ammoniated or aminated polycarboxylic acid chelating agent, the improvement providing for removal of iron oxides and copper in one operation while avoiding deposition of copper on the freshly cleaned metal substrate.
Other objects of the present invention will be more fully understood by those skilled in the art upon becoming familiar with the following description and the illustrative examples.
SUMMARY OF THE INVENTION The invention is based on the discovery that upon adding a polyamine having intralinear amino groups to an aqueous alkaline solution of an ammoniated or aminated polycarboxylic acid chelating agent, a new and improved metal cleaning solution is provided. Upon bringing such cleaning solution into contact with a ferrous metal surface having hardness and/or iron oxide scale, and copper, thereon and the solution being maintained at a temperature above about C. for a time sufficient to dissolve all the hardness and iron oxides, the copper is dissolved and neither precipitates from solution nor deposits on the ferrous metal surface.
BRIEF DESCRIPTION OF THE METHOD AND COMPOSITION OF THE INVENTION Any ferrous metal surfaces may be cleaned using the solution and method of the invention. Examples of such ferrous metals are cast iron, mild steel, and austenitic stainless steel.
Suitable polycarboxylic acid chelating agents include the alkylene polyamine polyacetic acids of the formula (HOOCCH,) N[(CH,),,N(CI-I COOH)],,,CI-I COOH wherein n is 1,2,3 or 4 and m is 0,l,2,3, or 4, up to two of the carboxymethyl groups may be replaced with a B-hydroxyethyl group and one or more of the carboxymethyl groups may be replaced by carboxyethyl groups. Specific examples of such polyacetic acids which are particularly suitable are ethylenediaminetetraacetic acid (EDTA), N-hydroxyethyl ethylenediaminetriacetic acid, nitrilotriacetic acid, N-2-hydroxyethyliminodiacetic acid, diethylenetriamine-pentaacetic acid, and mixtures thereof.
Such polycarboxylic acid chelating agents must be combined with ammonia or a suitable amine in order to obtain a solution with a basic pH. Solution pH can be further adjusted by the use of additional ammonia or amine.
Examples of suitable paired combinations of ammonia, amines, and alkanolamines with such polycarboxylic acids are listed in the following table.
Amine Pol carboxylic Acid ammonia EDTA ethanolamine EDTA ethylamine EDTA ethylenediamine EDTA diethylenetriamine EDTA pentaethylenehexamine EDTA dirnethylamine EDTA trimethylamine EDTA ethylenimine EDTA ethanolamine ethylenediaminetetrapropionic acid ethylenediamine N,N-di (fl-hydroxyethyl) glycine ammonia tetramethylenediamine- N,N,N',N'-tetraacetic acid ammonia (2-hydroxyethylimino) diacetic acid Any of the combinations of polycarboxylic acids and ammonia or amines considered together may be used in a concentration in the range of about 1 to 10 per cent by weight.
The polyamines which may be used are principally the polyalkylene polyamines having intralinear amino groups having a ratio of nitrogen atoms to carbon atoms in the chain of at least about 0.2 and preferably at least about 0.5. In addition, suitable polyamines must be readily soluble in the aqueous cleaning solution at an alkaline pH in the range of pH 7 to 10. Specific examples of suitable polyamines are polyethylenimine having molecular weights in the range of about 600 to 500,000, the reaction product of ethylenediamine and ethylenedichloride having an average molecular weight above about 230, preferably about 600 to 500,000, copolymerized N-phenyl ethylenimine and ethylenimine,
the copolymer having an n-phenyl group on about 10 per cent of the ethylene units in the molecule, and pentaethylenehexamine. The polyamines are employed in a concentration range of about 0.2 to per cent by weight. In any event, a sufficient amount of the polyamine must be used to provide two nitrogen atoms for each copper ion which is to be complexed. The amount of polyethylenimine to meet this requirement is about 2.8 parts per part by weight of copper.
Preferably, the corrosive attack of the polycarboxylic acid chelating agent upon the metal substrate is inhibited by an inhibitor compound or composition that does not interfere with the action of the present polyamines in keeping copper from plating out on the substrate. Examples of suitable inhibitors include, e.g. sodium mercaptobenzothiazole, di-aminoethylsulfide, or the product of the reaction of (1) one mole of an ammonia derivative having at least one hydrogen attached to nitrogen and having no groups reactive under the conditions of reaction other than hydrogen, (2) from 1.5 to moles of a ketone having at least one hydrogen atom on the carbon atom adjacent to the carbonyl group, (3) from 2 to 10 moles of an aldehyde selected from the group consisting of aliphatic aldehydes having from 1 to 16 carbon atoms and aromatic aldehydes of the benzene series and having no functional groups other than aldehyde groups, and (4) from 0.6 to 24 parts by weight based on (1), (2), and (3) of a fatty acid having from one to 20 carbon atoms at a temperature of from 150F. to about 250F for from 1 to 16 hours, such reaction product being more fully described in U.S. Pat. No. 3,077,454, which is expressly incorporated herein by reference, or mixtures thereof.
in carrying out the improved process as on a boiler system, the system is drained and then refilled with an aqueous alkaline solution of the polycarboxylic acid chelating agent having the polyamine dissolved therein. The aqueous solution is heated up in order to dissolve iron oxide or hardness deposits at practical rates. The solution is also heated in order to activate the polyamine. For the latter purpose, temperatures above about 155C are employed. Suitable temperatures are in the range of 155 to 190C. Normally the system is closed and the cleaning solution builds up some autogenous pressure due to the water and the ammonia or other volatile amine present. Pressure of the order of 20 to 200 pounds per square inch gauge are typical, but have no particular effect on the present method. The temperature of the cleaning solution is maintained for at least 30 to 60 minutes, or until the iron oxides and other deposits are removed. The process seldom takes more than 4 hours. At the end of this time the cleaning solution is drained and rinsed leaving a clean ferrous metal surface free of copper deposits.
In another embodiment of the present method the polyamine is activated by heating an aqueous solution thereof prior to adding the polyamine to the aqueous alkaline cleaing solution containing the polycarboxylic acid chelating agent. Heating about 10 per cent by weight aqueous solution of the polyamine to a temperature of at least 155C. and preferably 160 to 190C. for 30 minutes provides sufficient pyrolytic activation of the polyamine. With such prior activation outside the system to be cleaned, the cleaning of the ferrous metal surface may proceed at a much lower temperature, usually in the range of 110 to 150C. The advantage of using such lower temperature is decreased corrosion of the ferrous metal surface by the cleaning solution, without in any way interfering with the removal of copper deposits.
The following examples serve to illustrate the invention and not to limit the scope thereof.
EXAMPLE I An aqueous solution was prepared containing 3.8 per cent by weight of triammonium (ethylenedinitrilo) tetraacetate (ammoniated EDTA), 0.3 per cent by weight of polyethylenimine having a molecular weight of about 40,000 to 60,000, 0.05 per cent by weight of sodium mercaptobenzothiazole and 0.1 per cent by weight of a commercial inhibitor of the class described in U.S. Pat. No. 3,077,454 and consisting of the product of reaction of Rosin Amine D, tall oil fatty acids, acetophenone, and paraformaldehyde at a temperature of about C. for about 8 hours in ethylene glycol medium and in the presence of H 80 After the reaction, an adduct of nonylphenol and ethylene oxide was added to the reaction product all as more fully described in said U.S. patent.
A 200 milliliter quantity of this solution was placed in a glass beaker along with two 1010 (AISI) steel coupons having a natural mill-scale surface thereon. 0.3 grams of copper powder admixed with 0.7 grams of ferric oxide powder were also placed in the same glass beaker. The beaker and contents were placed in a pressure vessel. The vessel was closed and heated to 187C. The autogenous pressure in the vessel rose to pounds per square inch gauge. After 4 hours at the stated temperature the reactor was quenched with water and opened. The beaker and contents were removed. The coupons were found to be bright and clear and free of copper deposits.
COMPARISON TEST In an experiment made by way of comparison, a run was carried out as described in Example 1 except that the polyethylenimine was omitted from the aqueous cleaning solution. When the coupons were removed from the pressure vessel they were found to be free of mill-scale but heavily coated with copper.
EXAMPLE 2 On carrying out a run in the same manner as Example 1 except that a polyethylenimine having 10 per cent phenyl substitution in the molecule was substituted weight-by-weight for the polyethylenimine of example 1, the mill-scale coated coupons were cleaned and copper did not deposit on the cleaned surfaces.
EXAMPLE 3 On carrying out a run in the same manner as Example 1 except for the substitution of a linear polyalkylene polyamine for polyethylenimine the mill-scale coupons came out bright and clean and free of copper deposits.
COMPARlSON TEST In a run made by way of comparison, all conditions and reactants were the same as in example 1 except that the pressure vessel and contents were heated only to 119C. The coupons were cleaned of mill-scale but carried heavy copper deposit.
COMPARISON TEST In a run made by way of comparison, all conditions and reactants were the same as in example 1 except that the pressure vessel and contents were heated only to 140C. The coupons were cleaned of mill-scale but carried a heavy copper deposit.
EXAMPLE 4 A solution containing 3.8 per cent by weight of triammonium (ethylenedinitrilo)tetraacetate, and 0.25 per cent by weight of a polyethylenimine having a molecular weight of approximately 50,000 was prepared and 200 milliliters of this solution was placed in a glass beaker along with two 1010(AIS1) steel coupons which had been cleaned in nitric acid, dried and weighed. The beaker and contents were placed in a pressure vessel and heated to 150C. The temperature was maintained for 4 hours after which the pressure vessel was quenched and opened. The coupons were dried and weighed and corrosion of the metal was found to have taken place at the rate of 0.0605 pounds per square foot per day (lb/ftF/day).
EXAMPLE 5 When the test as in Example 4 was conducted using magnetite-coated coupons instead of acid cleaning coupons, the corrosion rate was found to be 0.0326 lb/ftF/day.
EXAMPLE 6 A run was carried out in the same manner as example 5 except that sodium mercaptobenzothiazole and the commercial inhibitor described in example 1 were added to the last solution in the same proportions as in Example 1. The coupons subject to test corroded at a rate of 0.0043 lb/ftF/day.
EXAMPLE 7 A solution containing 3.8 per cent by weight of triammonium (ethylenedinitrilo)tetraacetate and 0.3 per cent by weight polyethylenimine and 0.15 per cent by weight copper oxide was prepared and 200 milliliters of this solution was placed in a glass beaker. The beaker was placed in a pressure vessel and the vessel and contents were heated to 160C for about 30 minutes. The pressure vessel was then cooled and opened and two 1010(AIS1) steel coupons having a surface covered with mill-scale were placed in the beaker. The pressure vessel was then closed and heated to l C. The temperature was maintained for 4 hours, after which the pressure vessel was cooled and opened and the coupons examined. The coupons were found to be free of copper plating and they showed corrosion had taken place at the rate of 0.0173 lb/ftlday.
COMPARISON TEST On carrying out a run in about the same manner as Example 7 except that the inhibitors of Example 1 were added to the cleaning solution, initial heating was carried out at 165C. and the preheated cleaning solution was transferred anaerobically to another pressure vessel containing the two mill-scaled coupons, and the second pressure vessel was heated only to 97C. during the 4 hour period. The coupons under test were cleaned of millscale and showed that corrosion had taken place at a rate of 0.0091 1b./ft /day, but copper had plated out on the coupons.
The method and composition of the invention having been thus fully described various modifications thereof will at once be apparent to those skilled in the art and scope of the invention is to be considered limited only by the breadth of the claims hereafter appended.
We claim:
1. 1n the method of cleaning a ferrous metal surface, in the presence of metallic copper or dissolved copper by contacting the surface with an aqueous solution of an alkylene polyamine polyacetic acid chelating agent containing sufficient ammonia or amine to bring the solution pH in the range of about 7 to 10, the improvement which comprises:
adding a polyalkylenepolyamine to the aqueous cleaning solution prior to contacting the ferrous metal surface and maintaining the resulting aqueous cleaning solution at a temperature above about 155C. during at least the initial stage of the cleaning process, thereby preventing copper from depositing on the ferrous metal surface,
the polyalkylenepolyamine having an average molecular weight in the range of about 40,000 to 60,000 and being selected from the group consisting of polymerized ethylenimine, the reaction product of ethylenediamine and ethylenedichloride, and copolymerized N-phenyl ethylenimine and ethylenimine having an N-phenyl group on about 10 per cent of the ethylene units in the molecule.
2. The improvement as in claim 1 in which the aqueous cleaning solution is initially heated to a temperature in the range of above about 155 and up to 190C, and then the temperature is reduced to about 1 10 to C for the balance of the cleaning period.
3. The improvement as in claim 1 in which the cleaning solution contains from 0.1 to 5 per cent by weight of polyalkylenepolyamine, the cleaning solution is activated by heating to a temperature in the range of above about and up to C and thereafter the cleaning solution is maintained in contact with the ferrous metal surface at a temperature in the range of 1 10 to 150C.
4. The improvement as in claim 1 in which the total amount of polyalkylenepolyamine added to the aqueous solution is about 2.8 parts by weight per part of copper impurity present in the system being cleaned.
2 3 UNITED STATES PATENT OFFICE CERTIFICATE OF CORRECTIQN Patent No. "3,754,990 Dated August 28, 1973 I Fred N. Teumac & James S. Scruggs It is certified that error appears in the above-identified patent and that said Letters Patent are hereby corrected as shown below:
f Page 1, under References Cited, United States Patents, add
the following reference:
3,637, 508 1/72 Willsey et al. 134/41 xr Signed and sealed this 29th day of January 1974.
(SEAL) A ttest: EDWARD M.FLETCHER,JR. RENE D. TEG TMEYER Attesting Officer Acting Commissioner of Patents
Claims (3)
- 2. The improvement as in claim 1 in which the aqueous cleaning solution is initially heated to a temperature in the range of above about 155* and up to 190*C, and then the temperature is reduced to about 110* to 150*C for the balance of the cleaning period.
- 3. The improvement as in claim 1 in which the cleaning solution contains from 0.1 to 5 per cent by weight of polyalkylenepolyamine, the cleaning solution is activated by heating to a temperature in the range of above about 155* and up to 190*C and thereafter the cleaning solution is maintained in contact with the ferrous metal surface at a temperature in the range of 110* to 150*C.
- 4. The improvement as in claim 1 in which the total amount of polyalkylenepolyamine added to the aqueous solution is about 2.8 parts by weight per part of copper impurity present in the system being cleaned.
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US70426568A | 1968-02-09 | 1968-02-09 | |
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US3262791A (en) * | 1960-08-04 | 1966-07-26 | Petrolite Corp | Corrosion preventing method and composition |
US3067070A (en) * | 1961-02-01 | 1962-12-04 | Charles M Loucks | Cleaning method for industrial systems |
US3308065A (en) * | 1963-07-22 | 1967-03-07 | Dow Chemical Co | Scale removal, ferrous metal passivation and compositions therefor |
US3440170A (en) * | 1964-06-09 | 1969-04-22 | Ver Kunstmestf Mekog Albatros | Process for the cleaning of equipment |
US3438901A (en) * | 1965-10-22 | 1969-04-15 | Neiko I Vassileff | Metal treating bath and chelating agent for metal reactive acid baths |
US3490741A (en) * | 1966-09-15 | 1970-01-20 | Dow Chemical Co | Method of cleaning metal surfaces with polycarboxylic acid complexing agents inhibited by ethyleneimines or polyethylenepolyamines containing divalent sulfur |
US3447965A (en) * | 1966-10-31 | 1969-06-03 | Dow Chemical Co | Removal of copper containing scale from ferrous surfaces |
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US4020016A (en) * | 1975-02-28 | 1977-04-26 | The Drackett Company | Cleaning compositions effective in dissolving soap curd |
GB2157322A (en) * | 1984-03-29 | 1985-10-23 | Diversey Limited | Removal of iron oxide deposits |
US4720306A (en) * | 1985-04-16 | 1988-01-19 | Kraftwerk Union Aktiengesellschaft | Cleaning method |
US4721532A (en) * | 1985-08-05 | 1988-01-26 | W. R. Grace & Co. | Removal of iron fouling in cooling water systems |
US4778655A (en) * | 1985-10-29 | 1988-10-18 | W. R. Grace & Co. | Treatment of aqueous systems |
US4880568A (en) * | 1987-08-19 | 1989-11-14 | Aqua Process, Inc. | Method and composition for the removal of ammonium salt and metal compound deposits |
US4793865A (en) * | 1987-08-19 | 1988-12-27 | Aqua Process, Inc. | Method and composition for the removal of ammonium salt and metal compound deposits |
WO1993015177A1 (en) * | 1992-01-30 | 1993-08-05 | Casco Nobel Ab | Cleaning of equipment with respect to amino resins |
US5779814A (en) * | 1994-03-17 | 1998-07-14 | Fellers, Sr.; Billy Dean | Method for controlling and removing solid deposits from a surface of a component of a steam generating system |
US6017399A (en) * | 1994-03-17 | 2000-01-25 | Calgon Corporation | Method for controlling and removing solid deposits from a surface of a component of a steam generating system |
US6695927B1 (en) * | 1998-05-22 | 2004-02-24 | Siemens Aktiengesellschaft | Method and cleaning solution for cleaning a container |
US20060112972A1 (en) * | 2004-11-30 | 2006-06-01 | Ecolab Inc. | Methods and compositions for removing metal oxides |
US7611588B2 (en) | 2004-11-30 | 2009-11-03 | Ecolab Inc. | Methods and compositions for removing metal oxides |
US20070187646A1 (en) * | 2006-02-16 | 2007-08-16 | Fellers Billy D | Surface-active amines and methods of using same to impede corrosion |
US20130072418A1 (en) * | 2010-05-28 | 2013-03-21 | Mitsubishi Heavy Industries, Ltd. | Method for treating scales |
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