Title of Invention	A STABILISER FOR AQUEOUS ACIDIC HYDROGEN PEROXIDE AND A PROCESS FOR TREATING A METAL SURFACE WITH AN ACIDIC SOLUCTION
Abstract	"A stabiliser for aqueous acidic hydrogen peroxide and a process for treating a metal surface with an acidic solution: Aqueous acidic solutions of hydrogen peroxide used for metal surface treatments suffer from an increased decomposition rate of the hydrogen peroxide, caused by the dissolved metals such as iron, copper or titanium. Stabilisation can be achieved by employing a combination of a) a hydroxybenzoic acid, preferably p-hydroxy benzoic acid, b) a hydtrotropic sulphonic acid, preferably p-toluene sulphonic acid and c) a hydrophobic alkaryl sulphonic acid, preferably dodecylbenzene sulphonic acid in a weight ratio of a] ; b) : c) of 80-200, 50-1 20 and 2.5-6. Most desirably, the stabiliser is present at a concentration of 3-10 g/l in 35-70% hydrogen peroxide solution introduced into the aqueous acidic metal treatment solution.

Title of Invention

A STABILISER FOR AQUEOUS ACIDIC HYDROGEN PEROXIDE AND A PROCESS FOR TREATING A METAL SURFACE WITH AN ACIDIC SOLUCTION

Abstract

"A stabiliser for aqueous acidic hydrogen peroxide and a process for treating a metal surface with an acidic solution: Aqueous acidic solutions of hydrogen peroxide used for metal surface treatments suffer from an increased decomposition rate of the hydrogen peroxide, caused by the dissolved metals such as iron, copper or titanium. Stabilisation can be achieved by employing a combination of a) a hydroxybenzoic acid, preferably p-hydroxy benzoic acid, b) a hydtrotropic sulphonic acid, preferably p-toluene sulphonic acid and c) a hydrophobic alkaryl sulphonic acid, preferably dodecylbenzene sulphonic acid in a weight ratio of a] ; b) : c) of 80-200, 50-1 20 and 2.5-6. Most desirably, the stabiliser is present at a concentration of 3-10 g/l in 35-70% hydrogen peroxide solution introduced into the aqueous acidic metal treatment solution.

Full Text	This invention concerns metal surface treatment and in particular a process for metal surface treatment employing hydrogen peroxide in aqueous acidic solution, a solution containing hydrogen peroxide for treating metal surfaces and a stabiliser system for stabilising hydrogen peroxide. During metal processing, a metal oxide layer is often formed over all or part of the metal surface, impairing its appearance and/or suitability for further processing steps. Thus, for example, such a problem can arise for steel, including stainless steel, titanium and its alloys, copper and its alloys and even in some circumstances for aluminium. Accordingly, it is desirable to remove or at least reduce the size and extent of the metal oxide layer. Such processes can be described as metal surface cleansing, or in some instances more particularly as metal pickling or polishing or desmutting depending on the specific treatment being carried out. In one class of processes, a solution of hydrogen peroxide is employed, and often an aqueous acidic solution to remove the oxide layer. During the course of the metal surface treatment, the removal of the oxide layer causes metal to pass into solution. It is uneconomic and wasteful of resources to discard metal treatment solutions frequently, so that over the course of time, the concentration of metal in solution increases. The metals which pass into solution are usually the commonly employed metals such as iron, copper and metals alloyed with them such as nickel, chromium and titanium. Also, in some treatment processes such as in steel pickling, it is often the metal, ie iron, in solution which carries out much of the oxidation, and accordingly a significant concentration if the metal is deliberately maintained from the start of the process. These metals in acidic solution catalyse the decomposition of hydrogen peroxide so that it is desirable to find means of minimising the rate and/or extent to which the hydrogen peroxide decomposes. In order to retard peroxide decomposition in acidic solution, it has been proposed hitherto to include a number of different Inorganic or organic substances, which can often be alternatively described as chelating agents or free radical inhibitors. Without being limited to the particular mechanism by which stabilisation, ie peroxide decomposition retardation, is achieved, a number of the stabilisers can be described chemically as alcohols (USP 3869401, USP 3556883), carboxylic acids (USP3537895), phosphonic acids (USP 3122417 USP 4059678) or sulphonic acids (USP 3801512). Amongst the lists of stabilisers proposed for acid solutions, phydroxybenzoic acid has been disclosed in WO91/5079 (Solvay Interox Limited). It is a first object of certain aspects of the present invention to provide stabilisation means for aqueous acidic solutions of hydrogen peroxide, hydrogen peroxide solutions so stabilised and the use of such solutions for treating metals. It is a second object of further or related aspects of the present invention to provide means for augmenting or improving the stabilisation of hydrogen peroxide using a hydroxybenzoic acid, hydrogen peroxide solutions so stabilised and their use for treating metals. According to the present invention, there is provided a stabiliser for aqueous acidic hydrogen peroxide including a hydroxybenzoic acid characterised in that it comprises a) from 80 to 200 parts and preferably 100 tol 50 parts by weight of a hydroxybenzoic acid b) from 50 tol 20 parts and preferably from 60 to 100 parts by weight of a hydrotropic aryl sulphonic acid c) from 2.5 to 6 parts and preferably from 3 to 5 parts by weight of a hydrophobic alkaryl sulphonic acid. Herein by the termhydroxybeozoic acid is meant an aryl groupsubstituted by at least one hydroxy group and by a carboxylic acid group in any position relative thereto. A particularly suitable compound within the term comprises p-hydroxybenzoic acid. Herein by the term hydrotropic aryl sulphonic acid is meant an aryl group that is substituted by at least one short chain alkyl group and a sulphonic acid group in any position relative thereto and containing not more than 9 carbon atoms in total. A particularly suitable example, by virtue of its ready availablility and effectiveness is p-toluene sulphonic acid. Herein by the term hydrophobic alkaryl sulphonic acid is meant an aryl sulphonic acid which is substituted by a hydrophobic alkyl group containing at least 8 carbons. Said alkyl group often contains from 10 to 20 linear carbons, usually unbranched, and in many instances from 10 to 14 carbons or mixtures, such as dodecyl or mixtures averaging aboutl 2 carbons. A particularly suitable example is dodecylbenzene sulphonic acid, which often contains also a fraction of decyl, undecyl, terdecyl and tettadecyl groups. In particularly preferred stabiliser compositions, the weight ratio of each of components a) : b) : c) is selected in therange of 30 : 20 : 1, + /20%. In a number of related compositions containing preferred ratios, the weight ratio of component a) to component b) tocoiriponent c) is selected in the range of 18 to 25:20:0.8 to 1.2. By the employment of the three components together In ttie amounts and ratios disclosed above, and especially using preferred or especially ratios of the components, it is possible to obtain improved stabilisation of hydrogen peroxide in acidic solutions compared with the use of the hydroxybenzoic acid alone. Accordingly, the stabiliser of the present invention is particularly beneficial in those circumstances in which free hydrogen peroxide is maintained in solution. Although the three components of the stabiliser are referred to as the respective acids, it will be recognised herein for each of components a), b) and c) this includes employing or introducing the component as the corresponding saU thereof for all or part of each component of the stabiliser. In use, the acidity of the metal treatment solution will dictate the chemical form and extent of ionisation of the respective component therein. To the extent that a salt is employed, such as an alkali metal (sodium) salt, then its weight is as calculated as the corresponding acid. If desired, the compositions can be at least partially neutralised by the introduction of a water-soluble alkali such as an alkali metal hydroxide, eg sodium hydroxide. According to a second aspect of the present invention there are provided acidic metal treatment solutions containing or into which is introduced hydrogen peroxide, and containing or into which is introduced a stabiliser characterised in that the stabiliser comprises a) from 80 to 200 parts and preferably 100 tol 50 parts by weight of a hydroxybenzoic acid b) from 50 to 120 parts and preferably from 60 to 100 parts by weight of a hydrotropic aryl sulphonic acid c) from 2.5 to 6 parts and preferably from 3 to 5 parts by weight of a hydrophobic alkaryl sulphonic acid. The acidity in the aqueous metal treatment solutions is typically provided by one or more mineral acids and particilarly acids selected from sulphuric, phosphoric, hydrofluoric and hydrochloric acids, the selection being made at the discretion of the person wishing to conduct a metal treatment and taking into account which acids and mixtures thereof at what concentrations are suitable for the metal being treated. Additionally, if desired, a fraction of the acidity can be provided by nitric acid. The solutions intended for metal surface treatment are conventionally formulated to have a measured pH of 2 or lower, and in many instances the pH is chosen In the region of from below pH O, eg pH-0.5 up to pH 1. It will be understood that the measured pH will arise from Hie interaction between the acids introduced and any other constituents in the solution. For example, and as is well know, HF complexes in solution with Fe cations releasing H + ions and thereby lowering the measured pH compared with a plain HF solution devoid of Fe ions. It will also be understood that the skilled man will select the acid concentrations dependent on the metal treatment operation being contemplated. The highest concentrations relate to metal pickling and lower concentrations relate to polishing operations. The concentrations of the various acids in the metal treatment bath are selected in many embodiments in the ranges Identified below, to provide in combination a suitable pH of 2 or below sulphuric acid and/or phosphoric acid up to 250g./l, and often from 2 to 50 g/1 for polishing and 50 to 200 g/1 for pickling hydrofluoric acid and/or hydrochloric acid up to lOOg/I and otten from 10 to 50 g/1 It will be recognised that for certain purposes, combinations of acids are particularly suitable. For example, for pickling steel, especially stainless steels, or titanium, it is desirable to employ sulphuric acid at a concentration of 50 fol 50 g/1 and hydrofluoric acid at a concentration of from 20 to 35 g/1. It will be recognised that when stainless steel is being treated, the stabiliser is particularly effective when the Iron in solution is complexes such as with fluoride. For pickling copper or desrautting aluminium, it is desirable to employ a sulphuric acid solution at a concentration of 100 to 250 g/1. The hydrogen peroxide in the acid solution can be consumed rapidly, for example if its primary function is to oxidise in situ a species such as ferrous ions, possibly maintaining a desired mole ratio between ferrous and ferric ions m solution. Alternatively, a positive hydrogen peroxide concentration can be maintained such as a concentration that is usually not greater than 100g/1, and in many instances is from 0.1 tol 20 g/1, depending on the metal treatment. For copper pickling, the peroxide concentration is often from 10 to 50g/I and for copper polishing from 50 tol 20 g/I, and for steel or titanium treatment, the concentration is often from 0.1 to 10 g/1. In iJie steel pickling solutions, there is often present ferric ions in solution at a concentration of between 15 andl 50 gA, most preferably complexes when a positive concentration of hydrogen peroxide is present too. In other pickling solutions, some residual ferrous iron remains, and in such solutions the hydrogen peroxide is consumed rapidly in oxidising ferrous iron, preferably also complexes so that the peroxide is transient and not maintained at a positive concentration. The concentration of the stabiliser in the acid solution (ie the total of components a), b) and c) calculated as the respective acid, is often provided in the range of from 50 ppm to lOg/1 and In many Instances is selected in the range of from 200 ppm to lg/1, it being recognised that the practical upper limit for component a), which typically contributes in the region of 50 to 60% by weight of the stabiliser, will often be dependent on the solution temperature, a higher temperature permitting a higher concentration. The skilled person can readily carry out trials to determine the most appropriate concentration of the stabiliser in solution, balancing the cost of additional stabiliser or saving from using less stabiliser against the corresponding stability of the hydrogen peroxide and hence, respectively, the saving from reducing its rate of decomposition or the cost of permitting it to decompose a little more quickly. Advantageously, it has been found that in the trials conducted hitherto, variation in stabiliser concentration has not affected the rate at which the solution carries out the metal treatment, so that the user can continue to employ the processing conditions determined for the use of corresponding solutions employing altemative stabilisation systems for the hydrogen peroxide, such as that available from Soivay Interox under their TradeMark S333. The stabiliser can, if desired, be added into the acidic metal treatment solutions separately from the hydrogen peroxide, possibly dissolved in one or other of the mineral acids added to maintain acidity, but most conveniently at least part of the stabiliser can be introduced via the hydrogen peroxide solution. For example asuitable initial concentration of stabiliser in the bath can be provided either by direct introduction of stabiliser or by recycle of a previously used bath liquor, often after an intervening treatment to lower the concentration of dissolved metal in the liquor, and an acceptable stabiliser level is thereafter obtained as a result of the stabiliser introduced in the hydrogen peroxide solution. In a further aspect of the present invention there are provided concentrated hydrogen peroxide solutions containing the stabilizer a) from 80 to 200 parts and preferably 100 tol 50 parts by weight of a hydroxybenzoic acid b) from 50 tol 20 parts and preferably from 60 to 100 parts by weight of a hydrotropic aryl sulphonic acid c) from 2.5 to 6 parts and preferably from 3 to 5 parts by weight of a hydrophobicalkaryl sulphonic acid at a concentration of from 3 to lOg/1. In such concentrated solutions, the concentration of hydrogen peroxide is often from 35 to 70% w/w. By incorporating the stabiliser in the hydrogen peroxide solution, the presence of the stabiliser in the desired ratio of components a) b) and c) can be ensured. This simplifies the treatment process since the process user no longer needs to monitor for stabiliser content. It will also be recognised that by incorporating the invention stabiliser in the hydrogen peroxide solution, Ae process carries a built-in mechanism to offset losses from solution caused bycarry-ocit of solution from the treatment bath on the work piece or by extraction by air or any other gas which some users may wish to employ to agitate the bath and/or provide a supplementary source of oxygen, and the subsequent replenishment of the bath solution with fresh acid that does not contain stabiliser. When the stabiliser is incorporated into the hydrogen peroxide solution, it can be convenient to monitor its pH, and adjust to a pH in the range of from 3.2 to 3.8, by for example the introduction of a soluble alkali such as sodium hydroxide. In a further aspect of the present invention, there are provided processes for treating metal surfaces in which a metal surface that is partly or completely covered with an oxide layer is brought into contact with an acidic solution of hydrogen peroxide and a stabiliser therefor at a concentration that is effective at stabilizing and maintained in contact until at least a fraction of the oxide layer has been removed characterised in that the stabiliser comprises a) from 80 to 200 parts and preferably 100 tol 50 parts by weight of a hydroxybenzoic acid b) from 50 tol 20 parts and preferably from 60 to 100 parts by weight of a hydrotropic aryl sulphonic acid c) from 2.5 to 6 parts and preferably from 3 to 5 parts by weight of a hydrophobic alkaryl sulphonic acid. The metal treatment processes can be conducted under the operating conditions and employing acid and hydrogen peroxide concentrations that have hitherto been described or used for carrying out the respective treatment, but using other stabilisers for stabilising the acidic metal treatment solution, such a hydroxybenzoic acid in conjunction with components different from b)T ci. The actual conditions employed will take into account the metal surface being treated, the concentrations of active constituents in the acid solution and the operating temperature. The acid solutions employed are often in accordance with or similar to the acid solutions described hereinabove. The process temperature is often in the region of from 20 to 80°C and for many operations is selected in the range of from 35 to dCC. The period of time that the metal surface remains in contact with the acidic solution depends on the factors identified above and often determined in practice by ranging trials or from prior use of corresponding acidic peroxide treatment solutions using a different stabilizer such as that available under the mark S333. In many instances, the contact time is selected in the region of from 30 seconds to 40 minutes. It will be recognised that in accordance with possible process variations, the hydrogen peroxide (and particularly hydrogen peroxide containing the stabiliser) can be introduced to maintain a predetermined electropotential, eg 350 to 400 mV relative to a calomel electrode for steel pickling, or to maintain a specified concentration of hydrogen peroxide in the solution or within a predetermined range of concentrations. Having described the invention in general terms, specific embodiments thereof are described in greater detail by way of example only. Example 1 In ttiis Example, a stabilised hydrogen peroxide solution was prepared suitable for employment in metal treatment processes. PHBA (phydroxybenzoic acid, 3g) was charged into aqueous hydrogen peroxide (35% w/w, 994g) and stirred at laboratory ambient until by eye the solids had dissolved. PTSA (p-toluene sulphonic acid, 2g) was likewise charged into the mixture with stirring and dissolved at ambient and thereafter DBSA (dodecylbenzene sulphonic acid, 10% w/w active material,lg) was gently stirred into the mixture to avoid frothing. The resultant composition contained 3 g/1 component a), 2 g/I component b) and 0.1 g/1 component c). Example 2 and Comparisons C3 to C7 In this Example and comparisons, the effectiveness of the invention stabiliser is demonstrated relative to its components In the presence of a metal in solution that decomposes hydrogen peroxide. An iron containing acid solution was prepared by dissolving ferrous sulphate (15 g/1 as Fe) in aqueous sulphuric acid(63 g/1) and sufficient HF to provide uncomplexed HF in solution at 25g/l. and hydrogen peroxide solution (35%) w/w containing respectively the stabiliser or components thereof) was introduced into the iron solution until the free hydrogen peroxide concentration (after oxidation of the ferrous to ferric iron) was 0.5% w/w. The hydrogen peroxide solution was produced by the process of Example 1 or the appropriate stages thereof. The complexing of the iron with HF generated FeFn complexes in solution so that the effective sulphuric acid concentration was approximately 110/1. The iron-containing solution was stored at 50', the concentration of hydrogen peroxide therein was monitored and by interpolation, the time for half to be lost was determined (half life, time). The composition of the stabiliser system employed and the results are summarised in Table 1 below. From Table 1, it can be seen that the Example composition was markedly superior to the components themselves and to sub-combinations of them. Examples 8 to 14 In these Examples, Example 2 was repeated, but at varying concentrations of the three components of the stabiliser, as summarized in Table 2 below. In this Example, steel 316 was pickled with fresh solutions of iron/sulphuric acid/HF/ stabilised hydrogen peroxide according to respectively Examples 8 to 14 at 50°C In each pickle trial, it was found that the pickling was complete after 52 minutes producing a most acceptable surface finish. Examples 16 to 19 In these Examples, copper and brass was treated in two stages, first with a pickle solution containing 10% sulphuric acid and stabilised hydrogen peroxide according to Example 1 at ambient temperature and secondly with a polish solution containing 0.3% sulphuric acid and the stabilised hydrogen peroxide according to Example 1 at ambient temperature for the time and with the results summarized in Table 3 below. WE CLAIM: 1. A stabiliser for aqueous acidic hydrogen peroxide containing hydrobenzoic acid comprising: (a) from 80 to 200 parts by weight of hydroxybenzoic acid, (b) from 50 to 120 parts by weight of a compound having an aryl group substituted by atleast one short chain alkyl group and a sulphonic acid group in any position relative thereto, and not more than 9 carbon atoms in total and (c) from 2.5 to 6 parts by weight of an aryl sulphonic acid which is substituted by a hydrophobic alkyl group containing at least 8 carbon atoms. 2. The stabiliser as claimed in claim 1, wherein it comprises (a) from 100 to 150 parts by weight of a hydroxybenzoic acid (b) from 60 to 100 by weight of a hydrotropic aryl sulphonic acid (c) from 3 to 5 parts by weight of a hydrophobic alkaryl sulphonic acid. 3. The stabiliser as claimed in claim 2, wherein it comprises components a):b):c) in a weight ratio of 30:20:1 +/- 20%. 4. The stabiliser as claimed in claim 1, wherein it comprises components a):b):c) in a weight ratio of 18 to 25:20:0.8 to 1.2. 5. The stabiliser as claimed in any of the preceding claims, wherein component a) is p-hydroxybenzoic acid. 6. The stabiliser as claimed in any of the preceding claims, wherein component b) is p-toluene sulphonic acid. 7. The stabiliser as claimed in any of the preceding claims, wherein component c) is dodecylbenzene sulphonic acid. 8. An acidic metal treatment solutions containing or into which is introduced hydrogen peroxide, and containing or into which is introduced the stabilizer as claimed in any of claims 1 to 7. 9. The acidic solution as claimed in claim 8, which contains at least one mineral acid to provide a pH of from-0.5 to 2. 10. The acidic solution as claimed in claim 8 or 9, which contains 50 to 150 g/1 sulphuric acid, from 20 to 35 g/1 HF and 15 to 150 g/l iron calculated as Fe, said composition usefu for treatment of steel. U. The acidic solution as claimed in claim 8 or 9, which contains 25 to 250 g/1 sulphuric acid. 12. The acidic solution as claimed in any of claims 8 to 11, wherein the hydrogen peroxide is present in solution at a concentation of from 0.05 to 120 g/1. 13. The acidic solution as claimed in any of claims 8 to 12, wherein the stabiliser is present at a concentration of at least 50ppm. 14. A stabilised hydrogen peroxide solution for introduction into acidic solutions for metal surface treatment containing the stabilser as claimed in any of claims 1 to7. 15. The stabilised hydrogen peroxide solution as claimed in claim 14, wherein concentration of hydrogen peroxide is from 35 to 70% w/w. 16. The stabilised hydrogen peroxide solution as claimed in claim 14 or 15, wherein said solution has a pH of 3.2 to 3.8 obtained by introduction of a soluble alkali. 17. A process for treating a metal surface with an acidic solution containing or into which is introduced hydrogen peroxide and stabilizer therefore in which a workpiece is brought into contact with the acidic solution and maintained in contact until a fraction of an oxide layer on the metal surface has been removed wherein said solution contains as stabiliser for the hydrogen peroxide a) from 80 to 200 parts and preferably 100 to 150 parts by weight of a hydroxybenzoic acid b) from 50 to 120 parts and preferably from 60 to 100 parts by weight of a hydrotropic aryl sulphonic acid c) from 2.5 to 6 parts and preferably from 3 to 5 parts by weight of a hydrophobic aUcaryl sulphonic acid. 18. The process as claimed in claim 17, wherein the hydrogen peroxide solution introduced into the acidic solution is in accordance with the composition as claimed in claim 15.

Full Text

This invention concerns metal surface treatment and in particular a process for metal surface treatment employing hydrogen peroxide in aqueous acidic solution, a solution containing hydrogen peroxide for treating metal surfaces and a stabiliser system for stabilising hydrogen peroxide.
During metal processing, a metal oxide layer is often formed over all or part of the metal surface, impairing its appearance and/or suitability for further processing steps. Thus, for example, such a problem can arise for steel, including stainless steel, titanium and its alloys, copper and its alloys and even in some circumstances for aluminium. Accordingly, it is desirable to remove or at least reduce the size and extent of the metal oxide layer.
Such processes can be described as metal surface cleansing, or in some instances more particularly as metal pickling or polishing or desmutting depending on the specific treatment being carried out. In one class of processes, a solution of hydrogen peroxide is employed, and often an aqueous acidic solution to remove the oxide layer.
During the course of the metal surface treatment, the removal of the oxide layer causes metal to pass into solution. It is uneconomic and wasteful of resources to discard metal treatment solutions frequently, so that over the course of time, the concentration of metal in solution increases. The metals which pass into solution are usually the commonly employed metals such as iron, copper and metals alloyed with them such as nickel, chromium and titanium. Also, in some treatment processes such as in steel pickling, it is often the metal, ie iron, in solution which carries out much of the oxidation, and accordingly a significant concentration if the metal is deliberately maintained from the start of the process. These metals in acidic solution catalyse the decomposition of hydrogen peroxide so that it is desirable to find means of minimising the rate and/or extent to which the hydrogen peroxide decomposes.
In order to retard peroxide decomposition in acidic solution, it has been proposed hitherto to include a number of different Inorganic or organic substances, which can often be alternatively described as chelating agents or free radical inhibitors. Without being limited to the particular mechanism by which stabilisation, ie peroxide decomposition retardation, is achieved, a number of the stabilisers can be described chemically as alcohols (USP 3869401,

USP 3556883), carboxylic acids (USP3537895), phosphonic acids (USP 3122417 USP 4059678) or sulphonic acids (USP 3801512).
Amongst the lists of stabilisers proposed for acid solutions, phydroxybenzoic acid has
been disclosed in WO91/5079 (Solvay Interox
Limited).
It is a first object of certain aspects of the present invention to provide stabilisation means for aqueous acidic solutions of hydrogen peroxide, hydrogen peroxide solutions so stabilised and the use of such solutions for treating metals.
It is a second object of further or related aspects of the present invention to provide means for augmenting or improving the stabilisation of hydrogen peroxide using a hydroxybenzoic acid, hydrogen peroxide solutions so stabilised and their use for treating metals.
According to the present invention, there is provided a stabiliser for aqueous acidic hydrogen peroxide including a hydroxybenzoic acid characterised in that it comprises a) from 80 to 200 parts and preferably 100 tol 50 parts by weight of a hydroxybenzoic acid b) from 50 tol 20 parts and preferably from 60 to 100 parts by weight of a hydrotropic aryl sulphonic acid c) from 2.5 to 6 parts and preferably from 3 to 5 parts by weight of a hydrophobic alkaryl sulphonic acid.
Herein by the termhydroxybeozoic acid is meant an aryl groupsubstituted by at least one hydroxy group and by a carboxylic acid group in any position relative thereto. A particularly suitable compound within the term comprises p-hydroxybenzoic acid.
Herein by the term hydrotropic aryl sulphonic acid is meant an aryl group that is substituted by at least one short chain alkyl group and a sulphonic acid group in any position relative thereto and containing not more than 9 carbon atoms in total. A particularly suitable example, by virtue of its ready availablility and effectiveness is p-toluene sulphonic acid.
Herein by the term hydrophobic alkaryl sulphonic acid is meant an aryl sulphonic acid which is substituted by a hydrophobic alkyl group containing at least 8 carbons. Said alkyl

group often contains from 10 to 20 linear carbons, usually unbranched, and in many instances from 10 to 14 carbons or mixtures, such as dodecyl or mixtures averaging aboutl 2 carbons. A particularly suitable example is dodecylbenzene sulphonic acid, which often contains also a fraction of decyl, undecyl, terdecyl and tettadecyl groups.
In particularly preferred stabiliser compositions, the weight ratio of each of components a) : b) : c) is selected in therange of 30 : 20 : 1, + /20%. In a number of related compositions containing preferred ratios, the weight ratio of component a) to component b) tocoiriponent c) is selected in the range of 18 to 25:20:0.8 to 1.2.
By the employment of the three components together In ttie amounts and ratios disclosed above, and especially using preferred or especially ratios of the components, it is possible to obtain improved stabilisation of hydrogen peroxide in acidic solutions compared with the use of the hydroxybenzoic acid alone. Accordingly, the stabiliser of the present invention is particularly beneficial in those circumstances in which free hydrogen peroxide is maintained in solution.
Although the three components of the stabiliser are referred to as the respective acids, it will be recognised herein for each of components a), b) and c) this includes employing or introducing the component as the corresponding saU thereof for all or part of each component of the stabiliser.
In use, the acidity of the metal treatment solution will dictate the chemical form and extent of ionisation of the respective component therein. To the extent that a salt is employed, such as an alkali metal (sodium) salt, then its weight is as calculated as the corresponding acid. If desired, the compositions can be at least partially neutralised by the introduction of a water-soluble alkali such as an alkali metal hydroxide, eg sodium hydroxide.
According to a second aspect of the present invention there are provided acidic metal treatment solutions containing or into which is introduced hydrogen peroxide, and containing or into which is introduced a stabiliser characterised in that the stabiliser comprises a) from 80 to 200 parts and preferably 100 tol 50 parts by weight of a hydroxybenzoic acid b) from 50 to 120 parts and preferably from 60 to 100 parts by weight of a hydrotropic aryl sulphonic

acid c) from 2.5 to 6 parts and preferably from 3 to 5 parts by weight of a hydrophobic alkaryl sulphonic acid.
The acidity in the aqueous metal treatment solutions is typically provided by one or more mineral acids and particilarly acids selected from sulphuric, phosphoric, hydrofluoric and hydrochloric acids, the selection being made at the discretion of the person wishing to conduct a metal treatment and taking into account which acids and mixtures thereof at what concentrations are suitable for the metal being treated.
Additionally, if desired, a fraction of the acidity can be provided by nitric acid. The solutions intended for metal surface treatment are conventionally formulated to have a measured pH of 2 or lower, and in many instances the pH is chosen In the region of from below pH O, eg pH-0.5 up to pH 1. It will be understood that the measured pH will arise from Hie interaction between the acids introduced and any other constituents in the solution. For example, and as is well know, HF complexes in solution with Fe cations releasing H + ions and thereby lowering the measured pH compared with a plain HF solution devoid of Fe ions. It will also be understood that the skilled man will select the acid concentrations dependent on the metal treatment operation being contemplated. The highest concentrations relate to metal pickling and lower concentrations relate to polishing operations.
The concentrations of the various acids in the metal treatment bath are selected in
many embodiments in the ranges Identified below, to provide in combination a suitable pH of
2 or below sulphuric acid and/or phosphoric acid up to 250g./l, and often from 2 to 50 g/1 for
polishing and 50 to 200 g/1 for pickling hydrofluoric acid and/or hydrochloric acid up to
lOOg/I and otten from 10 to 50 g/1
It will be recognised that for certain purposes, combinations of acids are particularly suitable. For example, for pickling steel, especially stainless steels, or titanium, it is desirable to employ sulphuric acid at a concentration of 50 fol 50 g/1 and hydrofluoric acid at a concentration of from 20 to 35 g/1. It will be recognised that when stainless steel is being treated, the stabiliser is particularly effective when the Iron in solution is complexes such as with fluoride. For pickling copper or desrautting aluminium, it is desirable to employ a sulphuric acid solution at a concentration of 100 to 250 g/1.

The hydrogen peroxide in the acid solution can be consumed rapidly, for example if its primary function is to oxidise in situ a species such as ferrous ions, possibly maintaining a desired mole ratio between ferrous and ferric ions m solution. Alternatively, a positive hydrogen peroxide concentration can be maintained such as a concentration that is usually not greater than 100g/1, and in many instances is from 0.1 tol 20 g/1, depending on the metal treatment. For copper pickling, the peroxide concentration is often from 10 to 50g/I and for copper polishing from 50 tol 20 g/I, and for steel or titanium treatment, the concentration is often from 0.1 to 10 g/1. In iJie steel pickling solutions, there is often present ferric ions in solution at a concentration of between 15 andl 50 gA, most preferably complexes when a positive concentration of hydrogen peroxide is present too. In other pickling solutions, some residual ferrous iron remains, and in such solutions the hydrogen peroxide is consumed rapidly in oxidising ferrous iron, preferably also complexes so that the peroxide is transient and not maintained at a positive concentration.
The concentration of the stabiliser in the acid solution (ie the total of components a), b) and c) calculated as the respective acid, is often provided in the range of from 50 ppm to lOg/1 and In many Instances is selected in the range of from 200 ppm to lg/1, it being recognised that the practical upper limit for component a), which typically contributes in the region of 50 to 60% by weight of the stabiliser, will often be dependent on the solution temperature, a higher temperature permitting a higher concentration. The skilled person can readily carry out trials to determine the most appropriate concentration of the stabiliser in solution, balancing the cost of additional stabiliser or saving from using less stabiliser against the corresponding stability of the hydrogen peroxide and hence, respectively, the saving from reducing its rate of decomposition or the cost of permitting it to decompose a little more quickly. Advantageously, it has been found that in the trials conducted hitherto, variation in stabiliser concentration has not affected the rate at which the solution carries out the metal treatment, so that the user can continue to employ the processing conditions determined for the use of corresponding solutions employing altemative stabilisation systems for the hydrogen peroxide, such as that available from Soivay Interox under their TradeMark S333.
The stabiliser can, if desired, be added into the acidic metal treatment solutions separately from the hydrogen peroxide, possibly dissolved in one or other of the mineral acids added to maintain acidity, but most conveniently at least part of the stabiliser can be introduced via the hydrogen peroxide solution. For example asuitable initial concentration of

stabiliser in the bath can be provided either by direct introduction of stabiliser or by recycle of a previously used bath liquor, often after an intervening treatment to lower the concentration of dissolved metal in the liquor, and an acceptable stabiliser level is thereafter obtained as a result of the stabiliser introduced in the hydrogen peroxide solution.
In a further aspect of the present invention there are provided concentrated hydrogen
peroxide solutions containing the stabilizer a) from 80 to 200 parts and preferably 100 tol 50
parts by weight of a hydroxybenzoic acid b) from 50 tol 20 parts and preferably from 60 to
100 parts by weight of a hydrotropic aryl sulphonic acid c) from 2.5 to 6 parts and preferably
from 3 to 5 parts by weight of a
hydrophobicalkaryl sulphonic acid at a concentration of from 3 to lOg/1.
In such concentrated solutions, the concentration of hydrogen peroxide is often from 35 to 70% w/w.
By incorporating the stabiliser in the hydrogen peroxide solution, the presence of the stabiliser in the desired ratio of components a) b) and c) can be ensured. This simplifies the treatment process since the process user no longer needs to monitor for stabiliser content. It will also be recognised that by incorporating the invention stabiliser in the hydrogen peroxide solution, Ae process carries a built-in mechanism to offset losses from solution caused bycarry-ocit of solution from the treatment bath on the work piece or by extraction by air or any other gas which some users may wish to employ to agitate the bath and/or provide a supplementary source of oxygen, and the subsequent replenishment of the bath solution with fresh acid that does not contain stabiliser.
When the stabiliser is incorporated into the hydrogen peroxide solution, it can be convenient to monitor its pH, and adjust to a pH in the range of from 3.2 to 3.8, by for example the introduction of a soluble alkali such as sodium hydroxide.
In a further aspect of the present invention, there are provided processes for treating metal surfaces in which a metal surface that is partly or completely covered with an oxide layer is brought into contact with an acidic solution of hydrogen peroxide and a stabiliser therefor at a concentration that is effective at stabilizing and maintained in contact until at least a fraction of the oxide layer has been removed characterised in that the stabiliser

comprises a) from 80 to 200 parts and preferably 100 tol 50 parts by weight of a hydroxybenzoic acid b) from 50 tol 20 parts and preferably from 60 to 100 parts by weight of a hydrotropic aryl sulphonic acid c) from 2.5 to 6 parts and preferably from 3 to 5 parts by weight of a hydrophobic alkaryl sulphonic acid.
The metal treatment processes can be conducted under the operating conditions and employing acid and hydrogen peroxide concentrations that have hitherto been described or used for carrying out the respective treatment, but using other stabilisers for stabilising the acidic metal treatment solution, such a hydroxybenzoic acid in conjunction with components different from b)T ci. The actual conditions employed will take into account the metal surface being treated, the concentrations of active constituents in the acid solution and the operating temperature. The acid solutions employed are often in accordance with or similar to the acid solutions described hereinabove.
The process temperature is often in the region of from 20 to 80°C and for many operations is selected in the range of from 35 to dCC. The period of time that the metal surface remains in contact with the acidic solution depends on the factors identified above and often determined in practice by ranging trials or from prior use of corresponding acidic peroxide treatment solutions using a different stabilizer such as that available under the mark S333. In many instances, the contact time is selected in the region of from 30 seconds to 40 minutes.
It will be recognised that in accordance with possible process variations, the hydrogen peroxide (and particularly hydrogen peroxide containing the stabiliser) can be introduced to maintain a predetermined electropotential, eg 350 to 400 mV relative to a calomel electrode for steel pickling, or to maintain a specified concentration of hydrogen peroxide in the solution or within a predetermined range of concentrations.
Having described the invention in general terms, specific embodiments thereof are described in greater detail by way of example only.
Example 1
In ttiis Example, a stabilised hydrogen peroxide solution was prepared suitable for employment in metal treatment processes. PHBA (phydroxybenzoic acid, 3g) was charged

into aqueous hydrogen peroxide (35% w/w, 994g) and stirred at laboratory ambient until by eye the solids had dissolved. PTSA (p-toluene sulphonic acid, 2g) was likewise charged into the mixture with stirring and dissolved at ambient and thereafter DBSA (dodecylbenzene sulphonic acid, 10% w/w active material,lg) was gently stirred into the mixture to avoid frothing. The resultant composition contained 3 g/1 component a), 2 g/I component b) and 0.1 g/1 component c).
Example 2 and Comparisons C3 to C7
In this Example and comparisons, the effectiveness of the invention stabiliser is demonstrated relative to its components In the presence of a metal in solution that decomposes hydrogen peroxide.
An iron containing acid solution was prepared by dissolving ferrous sulphate (15 g/1 as Fe) in aqueous sulphuric acid(63 g/1) and sufficient HF to provide uncomplexed HF in solution at 25g/l. and hydrogen peroxide solution (35%) w/w containing respectively the stabiliser or components thereof) was introduced into the iron solution until the free hydrogen peroxide concentration (after oxidation of the ferrous to ferric iron) was 0.5% w/w. The hydrogen peroxide solution was produced by the process of Example 1 or the appropriate stages thereof. The complexing of the iron with HF generated FeFn complexes in solution so that the effective sulphuric acid concentration was approximately 110/1.
The iron-containing solution was stored at 50', the concentration of hydrogen peroxide therein was monitored and by interpolation, the time for half to be lost was determined (half life, time).
The composition of the stabiliser system employed and the results are summarised in Table 1 below.

From Table 1, it can be seen that the Example composition was markedly superior to the components themselves and to sub-combinations of them.
Examples 8 to 14
In these Examples, Example 2 was repeated, but at varying concentrations of the three components of the stabiliser, as summarized in Table 2 below.

In this Example, steel 316 was pickled with fresh solutions of iron/sulphuric acid/HF/ stabilised hydrogen peroxide according to respectively Examples 8 to 14 at 50°C In each pickle trial, it was found that the pickling was complete after 52 minutes producing a most acceptable surface finish.
Examples 16 to 19
In these Examples, copper and brass was treated in two stages, first with a pickle solution containing 10% sulphuric acid and stabilised hydrogen peroxide according to Example 1 at ambient temperature and secondly with a polish solution containing 0.3% sulphuric acid and the stabilised hydrogen peroxide according to Example 1 at ambient temperature for the time and with the results summarized in Table 3 below.

WE CLAIM:
1. A stabiliser for aqueous acidic hydrogen peroxide containing hydrobenzoic
acid comprising:
(a) from 80 to 200 parts by weight of hydroxybenzoic acid,
(b) from 50 to 120 parts by weight of a compound having an aryl group substituted by atleast one short chain alkyl group and a sulphonic acid group in any position relative thereto, and not more than 9 carbon atoms in total and
(c) from 2.5 to 6 parts by weight of an aryl sulphonic acid which is substituted by a hydrophobic alkyl group containing at least 8 carbon atoms.
2. The stabiliser as claimed in claim 1, wherein it comprises
(a) from 100 to 150 parts by weight of a hydroxybenzoic acid
(b) from 60 to 100 by weight of a hydrotropic aryl sulphonic acid
(c) from 3 to 5 parts by weight of a hydrophobic alkaryl sulphonic acid.

3. The stabiliser as claimed in claim 2, wherein it comprises components a):b):c) in a weight ratio of 30:20:1 +/- 20%.
4. The stabiliser as claimed in claim 1, wherein it comprises components a):b):c) in a weight ratio of 18 to 25:20:0.8 to 1.2.
5. The stabiliser as claimed in any of the preceding claims, wherein component a) is p-hydroxybenzoic acid.
6. The stabiliser as claimed in any of the preceding claims, wherein component b) is p-toluene sulphonic acid.

7. The stabiliser as claimed in any of the preceding claims, wherein component c) is dodecylbenzene sulphonic acid.
8. An acidic metal treatment solutions containing or into which is introduced hydrogen peroxide, and containing or into which is introduced the stabilizer as claimed in any of claims 1 to 7.
9. The acidic solution as claimed in claim 8, which contains at least one mineral acid to provide a pH of from-0.5 to 2.
10. The acidic solution as claimed in claim 8 or 9, which contains 50 to 150 g/1 sulphuric acid, from 20 to 35 g/1 HF and 15 to 150 g/l iron calculated as Fe, said composition usefu for treatment of steel.
U. The acidic solution as claimed in claim 8 or 9, which contains 25 to 250 g/1 sulphuric acid.
12. The acidic solution as claimed in any of claims 8 to 11, wherein the hydrogen peroxide is present in solution at a concentation of from 0.05 to 120 g/1.
13. The acidic solution as claimed in any of claims 8 to 12, wherein the stabiliser is present at a concentration of at least 50ppm.
14. A stabilised hydrogen peroxide solution for introduction into acidic solutions for metal surface treatment containing the stabilser as claimed in any of claims 1 to7.

15. The stabilised hydrogen peroxide solution as claimed in claim 14, wherein concentration of hydrogen peroxide is from 35 to 70% w/w.
16. The stabilised hydrogen peroxide solution as claimed in claim 14 or 15, wherein said solution has a pH of 3.2 to 3.8 obtained by introduction of a soluble alkali.
17. A process for treating a metal surface with an acidic solution containing or into
which is introduced hydrogen peroxide and stabilizer therefore in which a
workpiece is brought into contact with the acidic solution and maintained in
contact until a fraction of an oxide layer on the metal surface has been removed
wherein said solution contains as stabiliser for the hydrogen peroxide
a) from 80 to 200 parts and preferably 100 to 150 parts by weight of a
hydroxybenzoic acid
b) from 50 to 120 parts and preferably from 60 to 100 parts by weight of a
hydrotropic aryl sulphonic acid
c) from 2.5 to 6 parts and preferably from 3 to 5 parts by weight of a
hydrophobic aUcaryl sulphonic acid.
18. The process as claimed in claim 17, wherein the hydrogen peroxide solution
introduced into the acidic solution is in accordance with the composition as
claimed in claim 15.

Documents:

2198-mas-1997 abstract duplicate.pdf

2198-mas-1997 abstract.pdf

2198-mas-1997 claims duplicate.pdf

2198-mas-1997 claims.pdf

2198-mas-1997 correspondence others.pdf

2198-mas-1997 correspondence po.pdf

2198-mas-1997 description (complete) duplicate.pdf

2198-mas-1997 description (complete).pdf

2198-mas-1997 form-19.pdf

2198-mas-1997 form-2.pdf

2198-mas-1997 form-26.pdf

2198-mas-1997 form-4.pdf

2198-mas-1997 form-6.pdf

2198-mas-1997 others.pdf

2198-mas-1997 petition.pdf

« Previous Patent

Next Patent »

Patent Number

201878

Indian Patent Application Number

2198/MAS/1997

PG Journal Number

08/2007

Publication Date

23-Feb-2007

Grant Date

08-Aug-2006

Date of Filing

03-Oct-1997

Name of Patentee

M/S. SOLVAY INTEROX LIMITED

Applicant Address

BARONET WORKS, BARONET ROAD, WARRINGTON, CHESHIRE WA4 6HB,

Inventors:

#	Inventor's Name	Inventor's Address
1	SARAH JANE COLGAN	NE20, CROASDALE DRIVE, BEECHWOOD, RUNCORN, CHESHIRE WA7 2RJ
2	COLIN FREDERICK MOCDONOGH	36 WILLOW LANE, APPLETON PARK, WARRINGTON, CHESHIRE WA4 5DZ
3	NEIL JOSEPH SANDERS	65, CHARLES CRESCENT, ECCLESTON, ST HELENS, WA10 5EA

PCT International Classification Number

C01B15/037

PCT International Application Number

N/A

PCT International Filing date

PCT Conventions:

#	PCT Application Number	Date of Convention	Priority Country
1	9620877.2	1996-10-07	U.K.