Marine paint.

0001This invention relates to marine anti-fouling paints generally used as top-coat paints for ships' hulls.

0002The growth of marine organisms on the sub-marine parts of a ship's hull increases the frictional resistance of the hull to passage through water, leading to increased fuel consumption and/or a reduction in the speed of the ship. Marine growths accumulate so rapidly that the remedy of cleaning and repainting as required is impractical. In general the extent of fouling is limited by applying to the hull a top-coat incorporating anti-fouling agents. The anti-fouling agents are biocides which are freed from the surface of the paint over a period in concentrations lethal to marine organisms on the hull's surface. The anti-fouling paint fails only when the concentration of biocide available at the paint surface falls below the lethal concentrations, and with marine paints up to two years' useful life can be expected. The better anti-fouling paints are thus effective in dealing with gross infestation of hulls for considerable periods but a top coat paint of a ship's sub-marine surface has irregularities from its method of application and is furthermore subject to break-down and delamination during service, increasing the roughness of the hull, so that the performance of the ship falls off even when fouling is prevented.

0003Our British patent specification 1,457,590 describes and claims a paint based on a film-forming copolymer containing units of a triorganotin salt of an olefinically unsaturated carboxylic acid. Upon contact with seawater it loses triorganotin ions by ion exchange with seawater. This generates a water-soluble resin which essentially is a copolymer salt formed as a result of the depletion in the copolymer organotin content and exchange with metal ions present in seawater. This gradual dissolution of the copolymer means that a fresh anti-fouling paint surface is continuously revealed, prolonging the time for which biocide release at the paint surface is maintained above the lethal concentration.

0004The paint of British patent specification 1,457,590 has the remarkable property that relatively moving seawater smooths the surface of the paint, removing excrescences composed of the paint. When it is painted on a ship, the painted sub-marine surface of the ship at least preserves its initial smoothness and may become smoother during the ordinary traffic of the ship, leading to improved efficiency. The smoothing of the paint is inevitably accompanied by the release of the triorganotin ions into the surrounding seawater. In most circumstances, this is useful because the triorganotin ions are effective anti-fouling agents. However, triorganotin compounds are both expensive and strongly biocidal and it would be desirable in many circumstances to reduce the usage of triorganotin groups or avoid them altogether while obtaining the benefits of the smoothing of the paint in service.

0005We have now found surprisingly that certain polymers of more simple acrylate esters can be used as the basis of marine paints which are gradually planed away as a ship moves through seawater.

0006A marine paint according to the present invention comprises a film-forming acrylic polymer and a metalliferous pigment which is sparingly soluble in seawater. The acrylic polymer comprises 20 to 100 per cent by weight of monomer units (A) selected from methyl acrylate and ethyl acrylate units, 0 to 45 per cent by weight of monomer units (B) of a triorganotin salt of an olefinically unsaturated carboxylic acid, and 0 to 80 per cent by weight of units (C) which are alkyl methacrylate units having 1 to 4 carbons in the alkyl group or styrene units, monomer units (A) and (B) and (C) forming at least 80 per cent by weight of the polymer and the balance of the polymer, if any, being units of at least one other olefinically unsaturated comonomer.

0007The film-forming polymers used in the present invention are slowly hydrolysed in seawater so that they are gradually removed by motion through seawater. No inactive layer develops at the surface of the paint, and the paint at least maintains its initial smoothness in the manner shown in Figures 2A to 2D of British patent specification 1,457,590.

0008In a preferred form of the invention the monomer units (A) form 30 to 100 per cent by weight of the acrylic polymer and the monomer units (A) and monomer units (C) together form at least 90 per cent, for example 100 per cent, by weight of the polymer. Such film-forming polymers which are free from monomer units (B) do not release biocidal groups into the seawater and should be used in conjunction with a biocide for marine fouling organisms. This can be chosen for the particular waters which the ship is likely to encounter. The biocide can be in the form of a sparingly soluble metalliferous pigment such as cuprous oxide or an organic biocide can be used in the paint.

0009The polymer preferably contains at least 10 per cent by weight of the monomer units (C) since such polymers form stronger films. The C_l-4 alkyl methacrylate units are preferred, particularly methyl methacrylate units. The olefinically unsaturated comonomer, if used, can be an acrylic monomer, for example propyl acrylate, amyl acrylate, hexyl acrylate, butyl acrylate, hexyl methacrylate, acrylonitrile or methacrylonitrile, or a vinyl monomer, for example vinyl acetate, vinyl propionate, vinyl butyrate, vinyl chloride or vinyl pyridine. The polymer can contain monomer units conferring increased water reactivity, particularly when the polymer contains a relatively high proportion of monomer units (C), which tend to inhibit dissolution of the polymer. For example the polymer can contain up to 20 per cent by weight o maleic or itaconic anhydride, acrylamide, methacrylamide or N-vinyl pyrrolidone units or up to 5 per cent by weight, preferably 2 per cent or less, of acrylic, methacrylic or itaconic acid units. Care must be taken to avoid gelation of the paint when using a copolymer containing free acid monomer units.

0010The paint of the invention can be one which releases biocidal triorganotin ions by hydrolysis from a polymer and is smoothed by passage through seawater, but which is more economical in the use of triorganotin. In this case the film-forming acrylic polymer preferably comprises 20 - 70 per cent by weight of monomer units (A), up to 45 per cent by weight, for example 10-45 per cent, of monomer units (B) and 20-50 per cent by weight of monomer units (C). The monomer units (B) are preferably of the formula R₃SnOOCCR' = _CHR" where each R is an alkyl radical containing 2 to 8 carbon atoms or an aryl or aralkyl radical, R' is H or CH₃ and R" is H or -COOSnR₃. The groups R attached to the tin atom can be different but are preferably the same, for example R₃Sn can be tributyl tin, tripropyl tin, tribenzyl tin, triphenyl tin, tritolyl tin or trihexyl tin. The carboxylate group -OOCCR' - CHR" is preferably acrylate, methacrylate or maleate.

0011The film-forming polymer can be prepared by addition polymerisation of the appropriate monomers in the appropriate proportions at polymerisation conditions using a free radical catalyst such as benzoyl peroxide or azobisisobutyronitrile in an organic solvent such as xylene, toluene, butyl acetate, n-butanol, 2-ethoxyethanol, cyclohexanone, 2-methoxyethanol, 2-butoxyethanol and/or 2-ethoxyethyl acetate. Polymerisation is preferably at a temperature in the range 70 - 100°C. Within this range the use of higher temperatures produces polymers of lower molecular weight. Polymerisation may be carried out by heating all the polymer ingredients in the solvent at the required temperature or by gradually adding a mixture of the monomers and catalyst to treated solvent. The latter procedure produces polymers of lower molecular weight. A chain transfer agent such as a mercaptan can also be used to produce polymers of lower molecular weight. For a given proportion of monomers the paint tends to dissolve in and become smoothed by relatively moving sea water more rapidly if the polymer has a lower molecular weight, and such polymers may be preferred when using a high proportion of monomer units (C), particularly if monomer units (C) comprise styrene.

0012Mixtures of polymers of different composition, or of higher and lower molecular weight polymers, can be used.

0013Alternatively the paint can be an aqueous emulsion paint based on a film-forming acrylic polymer prepared by emulsion polymerisation. In this case the monomers are preferably chosen so that the polymer has a glass transition temperature of 5-25⁰C. Emulsion copolymers preferably include no more than 40 per cent by weight of monomerunits (C).

0014The metalliferous pigment sparingly soluble in seawater is exemplified by cuprous thiocyanate, cuprous oxide, zinc oxide, cupric acetate meta-arsenate, zinc chromate, zinc dimethyl dithiocarbamate and zinc diethyl dithiocarbamate.

0015The paint preferably includes a least one metalliferous pigment selected from zinc oxide, cuprous oxide and cuprous thiocyanate and pigments whose seawater solubility is similar to theirs. These pigments have a seawater solubility such that the pigment particles do not survive at the paint surface. The pigment has the effect of inducing the overall smoothing which the relatively-moving seawater exerts on the paint film, minimising localised erosion and preferentially removing excrescences formed during the application of the paint. Mixtures of sparingly soluble pigments can be used, for example zinc oxide which is most effective at inducing the gradual dissolution of the paint,can be mixed with cuprous oxide, cuprous thiocyanate or zinc dimethyl dithiocarbamate which are more effective marine biocides.

0016Such mixtures preferably comprise up to 75 per cent by volume zinc oxide and 25-100 per cent by volume cuprous oxide or cuprous thiocyanate. Zinc dimethyl dithiocarbamate and zinc diethyl dithiocarbamate are somewhat less soluble than cuprous oxide or thiocyanate. If used, they preferably form up to 75 per cent by volume of the pigment, with at least 25 per cent by volume of the pigment being zinc oxide.

0017The paint composition can additionally contain a pigment which is highly insoluble in seawater, such as titanium dioxide or ferric oxide. Such highly insoluble pigments can be used at up to 40 per cent by weight of the total pigment component of the paint. The highly insoluble pigment has the effect of retarding the dissolution of the paint.

0018The proportion of pigment to polymer is generally such as to give a pigment volume concentration of at least 25 per cent, preferably at least 35 per cent, in the dry paint film. The upper limit of pigment concentration is the critical pigment volume concentration. Paints of pigment volume concentration about 50 per cent, for example, have been found very effective for smoothing in seawater and preventing fouling.

0019Paints according to the invention may include a plasticiser although this is not usually necessary. Examples of plasticisers are tritolyl phosphate, diisooctyl phthalate, tributyl phosphate, butyl benzyl phthalate, dibutyl tartrate, 'Lutenal A25' polyether and hydrophobic organic plasticisers which retard the rate of dissolution of the paint, such as chlorinated diphenyl, for example Aroclor 1254 sold by Monsanto Ltd., chlorinated paraffin wax, for example Cereclor 48 and Cereclor 70 sold by I.C.I. Ltd., diphenyl ether, dichloro-diphenyl-trichloroethane or low-molecular weight polybutenes such as Hyvis 05 sold by B.P. Ltd.

0020Many of the metalliferous pigments sparingly soluble in seawater have biocidal activity, particularly copper compounds such as cuprous thiocyanate, cupric acetate meta-arsenate and cuprous oxide, and also zinc oxide to a lesser extent. Even when the polymer contains no triorganotin salt units (B) the biocidal effect of these sparingly soluble pigments, particularly cuprous oxide, may be sufficient so that the paint needs no further biocide, for example for use on the flat bottom of very large tankers, where fouling is less likely to occur. We believe that the self-smoothing action of the paint increases its resistance to fouling compared to a conventional paint releasing biocide at the same rate; this effect is-more marked with increasing rate of dissolution of the paint, as for example when the film-forming polymer contains a high proportion of methyl or ethyl acrylate and the sparingly soluble pigment includes zinc oxide.

0021The paint can contain an added biocide effective against seaweed and barnacles. Triorganotin salts and oxides such as triphenyltin fluoride, tributyl tin fluoride, tributyl tin dibromosuccinate, triphenyltin chloride, triphenyltin hydroxide and tributyltin oxide are effective marine biocides and can be used in paints according to the invention, particularly where the polymer contains no monomer units (B). A paint according to the invention comprising a tin-free polymer, a pigment such as cuprous oxide and a small proportion of a triorganotin salt (up to 25 per cent by volume based on the pigment) may have antifouling and smoothing properties equal to an organotin copolymer paint of much higher total organotin content. Alternatively a mixture of organotin- free and organotin polymers can be used.

0022In some cases it will be desired to avoid completely the release of triorganotin ions. Examples of other biocides effective as antifouling agents are di-thiocarbamate derivatives such as cuprous ethylene bis-di-thiocarbamate or 2-(N,N-dimethyl thiocarbamyl thio)-5-nitro thiazole, substituted isothiazolones particularly halogenated N-substituted isothiazolones, tetramethyl thiuram disulphide and dichlorodi- phenyltrichloroethane (which also acts as a hydrophobic organic retarder).

0023The invention is illustrated by the following Examples:-

Example 1

0024Methyl methacrylate (7.6g; 0.076 mole) and methyl acrylate (68.4g; 0.795 mole) were dissolved in a mixture of xylene (85.4g) and cyclohexanone (36.6g). Azobisisobutyronitrile (AIBN) (2.0g; 0.012 mole) was added and the solution was heated to 80°C. The polymerisation reaction was conducted (with stirring) at this temperature. There was an exotherm in the first 20 minutes of the reaction. The course of the polymerisation was followed by monitoring the change in the refractive index. No further significant change was observed after 3 hours and the solution was then heated to 100°C for a period of 30 minutes to destroy any residual activity of AIBN.

0025The product was a 36.0 per cent by volume solids solution of a copolymer of 10 per cent by weight methyl methacrylate and 90 per cent by weight methyl acrylate.

002688.7 g of the copolymer solution produced above was mixed with cuprous oxide (71.5g) and Aerosil colloidal silica (1.3g) and milled overnight to produce a paint of pigment volume concentration 35 per cent.

Example 2

002788.7g of the copolymer solution produced as in Example 1 was mixed with cuprous thiocyanate (35.2g) and Aerosil colloidal silica (1.3g) and milled overnight.

Example 3

002888.7g of the copolymer solution produced as in Example ₁ was mixed with zinc oxide (33.8g), cuprous oxide (35.7g) and Aerosil colloidal silica (1.3g) and milled overnight. The paint contained Zn0:Cu₂0 in 50:50 ratio by volume.

Example 4

002988.7g copolymer solution produced as in Example 1 was mixed with zinc oxide (50.7g), cuprous oxide (17.9g) and Aerosil colloidal silica (1.3g) and milled overnight. The paint contained ZnO:Cu₂0 in 75:25 ratio, by volume.

0030The smoothing performance of paints in relatively moving seawater can be tested in the apparatus described in British Patent Specification 1,457,590 with reference to

0031Figures 7A and 7B. A disc having a diameter of 23 cm is coated in radial stripes with the paints under test. The stripes are applied by a standardised applicator adapted to deposit a film 20p thick (wet thickness). The disc is immersed in flowing seawater and rotated at a peripheral speed of 33 knots.

0032During this test the paint films under test are planed away, eventually to the extent that the underlying substrate is revealed. There is always some variation in the thickness of the paint film within each stripe so that the stripe of paint does not suddenly vanish; an increasing proportion of the substrate is revealed over time. When the substrate is revealed over 50 per cent of the area of the stripe it is a good approximation to say that the paint film in the stripe has lost by planing the original average dry thickness of the paint film in the stripe. The time in days to achieve this ("D⁵⁰") is a measure of the rate of planing of the paint in relatively moving seawater.

0033The surface of the paint film in each stripe should be examined during the test to note whther it is smooth and firm. Paint films according to the invention which at least retain their initial smoothness must be distinguished from paint films which are removed over at least a portion of the stripe by flaking or localised erosion causing roughening or by separation from the disc.

0034The above test can be used to give an absolute rate of planing of the paint film, but the temperature, composition and flow rate of the seawater can effect the result. The test is preferably used as a comparison in which one of the stripes painted on the disc is an antifouling paint known to have the desired rate of dissolution in relatively moving seawater.

0035A disc was prepared having 2 stripes each of the paints of Examples 1, 2 and 3, one stripe of the paint of Example 4, 2 stripes of a commercially successful self-polishing paint X and 2 stripes of paint Y comprising (by weight) 36.1 per cent of a 40 per cent by volume solution of a 60:40 tributyltin methacrylate/methyl methacrylate copolymer, 45.8 per cent ZnO, 0.7 per cent colloidal silica, 0.9 per cent bentonite, 0.4 per cent tributyltin oxide and 12.4 per cent xylene. This paint is known from British Patent Specification 1,457,590 to be smoothed away during motion through seawater at a dissolution rate which is generally too fast for optimum commercial use, but which can be retarded to the optimum rate by a hydrophobic organic material.

0036All the paints were observed to be planed away during rotation in seawater.

0037The stripes of comparison paint X had an average _D⁵⁰ of 15.5 days and those of comparison paint Y had a _D⁵⁰ of 3 days. The average D⁵⁰ of the paints of Examples 1, 2, 3 and 4 respectively were 17 days, 28 days, 9.5 days and 5.8 days. These results indicate that the paints of Examples 1, 2 and 3 have a rate of dissolution in relatively moving seawater which would be sufficient to give appreciable smoothing of the paint film but not too fast for commercial use. The paint of Example 4 dissolved somewhat faster than would be desired in commercial practice but slower than comparison paint Y, indicating that its dissolution could be retarded to a commercial rate by the addition of a minor amount of an organic hydrophobic retarder. All the rates of dissolution were compatible with the release of sufficient of an added biocide without forming a leached inactive outer layer of paint.

Example 5

0038Methyl methacrylate (22.8g; 0.228 mole) and methyl acrylate (53.2g; 0.619 mole) were dissolved in xylene (122g). AIBN (2.0g; 0.012 mole) was added and the solution was heated to 80°C. The polymerisation reation was conducted (with stirring) at this temperature. There was a mild exotherm in the first 20 minutes of the reaction. The course of the polymerisation was followed by monitoring the change in the refractive index. No further significant change was observed after 4 hours and the solution was then heated to 100°C for a period of 30 minutes to destroy any residual activity of AIBN. The product was a 37.6 per cent by volume solids solution of a copolymer of 30 per cent by weight methyl methacrylate and 70 per cent by weight methyl acrylate.

003984.4g of the copolymer solution priduced above was mixed with cuprous oxide (7.5g), Aerosil colloidal silica (1.3g) and xylene (1.5g) and milled overnight.

Example 6

004084.4g of the copolymer solution produced as in Example 5 was mixed with zinc oxide (33.8g), cuprous oxide (35.7g), Aerosil colloidal silica (1.3g) and xylene (1.5g) and milled overnight. The product contained ZnO : C_U20 in 50:50 ratio, by volume.

Example 7

0041Copolymer solution (84.4g) produced as in Example 5 was mixed with zinc oxide (50.7g), cuprous oxide (17.9g), Aerosil colloidal silica (1.3g) and xylene (1.5g) and milled overnight. The paint contained Zn0 : Cu₂0 in 75:25 ratio, by volume.

Example 8

0042A 36 per cent by volume solids solution of poly(methyl acrylate) in a 70:30 mixture of xylene and cyclohexanone was prepared by the procedure of Example 1. This solution was milled with cuprous oxide and 0.8 per cent by weight colloida silica to form a paint having a pigment volume concentration of 35 per cent and a solids content of 37 per cent by volume.

Examples 9 and 10

0043The poly(methyl acrylate) solution of Example 8 was milled with zinc oxide and cuprous oxide in differing proportions, and with 0.8 per cent by weight colloidal silica in each case to form two paints, each having a pigment volume concentration of 35 per cent and a solids content of 37 per cent by volume. The paint of Example 9 had ZnO : C_U20 ratio of 50:50 by volume and the paint of Example 10 had a ZnO : Cu₂0 ratio of 75:25 by volume.

Example 11

0044A 36 per cent by volume solids solution in xylene of a copolymer of 70 per cent by weight methyl methacrylate and 30 per cent by weight methyl acrylate was prepared by the procedure of Example 5. This solution was milled with zinc oxide and cuprous oxide and 0.8 per cent by weight colloidal silica to form a paint having a pigment volume concentration of 35 per cent, a ZnO : Cu₂O ratio of 75:25 by volume and a solids content of 37 per centby volume.

0045The paints of Examples 5 to 11 were tested in the rotating disc test described above. A disc was prepared having 2 stripes each of the paints of Examples 5, 6, 7 and 9, one stripe each of the paints of Examples 8, 10 and 11 and 2 stripes each of comparison paints X and Y described above.

0046All the paints were observed to be planed away during rotation in seawater.

0047The stripesof comparison paint X had a D⁵⁰ of 12 days and those of comparison paint Y had a D⁵⁰ of 2 days. The average D⁵⁰ of the paints of Examples 5 to 11 were as follows:- <tables id="tabl0001" num="0001"><img file="EP0051930A2_D0001.tif" /></tables>

0048These results indicate that the paints of Examples 5, 6, 8, 9 and 11 have a rate of dissolution in relatively moving seawater which would be sufficient to give appreciable smoothing of the paint film but not too fast for commercial use.

0049The paints of Examples 7 and 10 dissolved somewhat faster than would be desired in commercial practice but slower than comparison paint Y, indicating that their dissolution could be retarded to a commercial rate by the addition of a minor amount of an organic hydrophobic retarder. All the rates of dissolution were compatible with the release of sufficient of an added biocide without forming a leached inactive outer layer of paint.

Example 12

0050A copolymer of 10 per cent by weight methyl methacrylate and 90 per cent by weight methyl acrylate was prepared by the process described in Example 1, using a 4:1 by weight mixture of xylene and 2-ethoxy-ethyl acetate as solvent to produce a 39.6 per cent by volume solution. 124g of this copolymer solution was mixed with l48g cuprous oxide, 47g zinc oxide, 3g Aerosil colloidal silica, 5g bentonite, 2g n-butanol, 27g xylene and 7g 2-ethoxy-ethyl acetate to produce a paint of pigment volume concentration (P.V.C.) 50 per cent and a ratio of cuprous oxide to zinc oxide of 75:25 by volume.

Example 13

005140 per cent by weight methyl methacrylate and 60 per cent by weight methyl acrylate were copolymerised in xylene using the procedure described in Example 5 to produce a 42.2 per cent by volume copolymer solution. 146g of this solution was mixed with 83g cuprous oxide, 26g zinc oxide, 7g triphenyltin fluoride, 2g Aerosil colloidal silica, 3g bentonite, lg n-butanol and 22g xylene to produce a paint of P.V.C. 35 per cent.

Example 14

005210 per cent by weight methyl methacrylate and 90 per cent by weight ethyl acrylate were copolymerised in xylene using the procedure of Example 5 to produce a 39.6 per cent by volume copolymer solution. 117g of this copolymer solution was mixed with 198g cuprous oxide, 3g Aerosil colloidal silica, 5g bentonite, 2g n-butanol and 3.7g xylene to produce a paint of P.V.C. 50 per cent

Example 15

0053A paint was prepared as described in Example 14 except that 25 per cent of the cuprous oxide was replaced by an equal volume (47g) of zinc oxide.

Example 16

005470 per cent by weight methyl methacrylate and 30 per cent by weight ethyl acrylate were copolymerised in xylene using the procedure of Example 5 to produce a 43.9 per cent by volume copolymer solution. 136g of this copolymer solution was mixed with 28g cuprous oxide, 79g zinc oxide, 5g tributyltin fluoride, 2g Aerosil colloidal silica, 3g bentonite, lg n-butanol and 30g xylene to produce a paint of P.V.C. 35 per cent.

Example 17

0055195g methyl acrylate was polymerised in 204g xylene and 60g 2-ethoxy-ethyl acetate using 5g AIBN catalyst to produce a 39 per cent by volume solution of poly(methyl acrylate). 127g of this polymer solution was mixed with 148g cuprous oxide, 47g zinc oxide, 3g Aerosil colloidal silica, 5g bentonite, 23g xylene, 6g 2-ethoxy-ethyl acetate and 2g n-butanol to produce a paint of P.V.C. 50 per cent.

Example 18

0056123g of a 39.7 per cent by volume solution in xylene of a copolymer of 30 per cent by weight methyl methacrylate and 70 per cent by weight methyl acrylate prepared as described in Example 5 was mixed with 148g cuprous oxide, 47g zinc oxide, 3g Aerosil colloidal silica, 5g bentonite, 31g xylene and 2g n-butanol to produce a paint of P.V.C. 50 per cent.

Example 19

0057189g of the copolymer solution of Example 14 was mixed with 66g zinc oxide, 20g zinc dimethyl dithiocarbamate, 7g tributyltin fluoride, 2.5g Aerosil colloidal silica, 4g bentonite, 19g xylene and 1.5g n-butanol to produce a paint of P.V.C. 35 per cent.

Example 20

0058240g xylene was heated to 90°C. 14.8g methyl methacrylate, 133.2g methyl acrylate and 12g AIBN were mixed and the mixture was gradually added to the hot xylene over 1.5 hours. A 38.2 per cent by volume solution of a 10:90 by weight copolymer of methyl methacrylate:methyl acrylate was produced. 133g of this copolymer solution was mixed with l48g cuprous oxide, 47g zinc oxide, 3g Aerosil colloidal silica, 5g bentonite, 23g xylene and 2g n-butanol to produce a paint of P.V.C. 50 per cent.

Example 21

0059Methyl methacrylate and methyl acrylate were copolymerised in xylene by the procedure of Example 5 to produce a 41.6 per cent by volume solution of a 70:30 by weight methyl methacrylate:methyl acrylate copolymer. 141g of this copolymer solution was mixed with 113.5g cuprous oxide, 4.5g tributyltin oxide, 13g titanium dioxide, 2.5g Aerosil colloidal silica, 4.5g bentonite, 1.5g n-butanol and 20g xylene to produce a paint of P.V.C. 35 per cent.

Example 22

0060158.5g of the copolymer solution of Example 21 was mixed with 45g cuprous thiocyanate, 2g tributyltin oxide, 5.5g titanium dioxide, 13g talc, lg phthalocyanine blue, 2g Aerosil colloidal silica, 2.5g bentonite, 1.5g n-butanol and 8g xylene to produce a paint of P.V.C. 35 per cent.

Example 23

0061134.6g (69 per cent by weight) methyl methacrylate, 58.5g (30 per cent by weight) methyl acrylate and 2.0g (1 per cent by weight) methacrylic acid were copolymerised at 80°C for 3 hours in a mixture of 150g xylene and 150g cyclohexanone using 5g AIBN catalyst to produce a 43.6 per cent by volume copolymer solution. l40g of the copolymer solution was mixed with lllg cuprous oxide, 5.5g tributyltin fluoride, 2g Aerosil colloidal silica, 3.5g bentonite, 1.5g n-butanol, 15.5g xylene and 15.5g cyclohexanone to produce a paint of P.V.C. 35 per cent.

Examples 24 - 26

0062Copolymers were prepared by the process of Example 23 using the proportions of monomers listed below:- <tables id="tabl0002" num="0002"><img file="EP0051930A2_D0002.tif" /></tables>

0063Paints of P.V.C. 35 per cent were produced from each of the copolymers using the same pigment and other ingredients as in Example 23.

Example 27

0064300g xylene was heated to 90°C. 161g methyl acrylate was mixed with 29g styrene and lOg AIBN and added to the hot xylene over 1 hour. The mixture was held at 90°C for a further hour to produce a 38.2 per cent by volume solution of a 15:85 by weight styrene:methyl acrylate copolymer. 126g of the copolymer solution was mixed with 42.5g zinc oxide, 134.5g cuprous oxide, 2.5g Aerosil colloidal silica, 4.5g bentonite, 33.5g xylene and 1.5g n-butanol to produce a paint of P.V.C. 50 per cent.

Example 28

006576g styrene and 114g methyl acrylate were copolymerised using the procedure of Example 27 to produce a 35.-8 per cent by volume solution of a 40:60 by weight copolymer of styrene: methyl acrylate. 131g of the copolymer solution was mixed with 42.5g zinc oxide, 134.5g cuprous oxide, 2.5g Aerosil colloidal silica, 4.5g bentonite, 24g xylene and 1.5g n-butanol to produce a paint of P.V.C. 50 per cent.

Example 29

0066171g methyl acrylate and 19g methacrylamide were copolymerised in 300g cyclohexanone using lOg AIBN catalyst under the procedure of Example 1 to produce a 42.1 per cent by volume solution of a 90:10 by weight copolymer of methyl acrylate:methacrylamide. 136.5g of the copolymer solution was mixed with 147.5g cuprous oxide, 46.5g zinc oxide, 3g Aerosil colloidal silica, 5.5g bentonite, 1.5g n-butanol and 24g cyclohexanone to produce a paint of P.V.C. 50 per cent.

Example 30

006778g methyl methacrylate, 39g methyl acrylate and 78g tributyltin methacrylate were copolymerised in 222g xylene using 5g AIBN and the procedure of Example 5 to produce a 39.2 per cent by volume solution of a 40:20:40 by weight copolymer of methyl methacrylate:methyl acrylate:tributyltin methacrylate. 163g of this copolymer solution was mixed with 66g zinc oxide, 69.5g cuprous oxide, 2g Aerosil colloidal silica, 3.5g bentonite, 1.3g n-butanol and 7g xylene to produce a paint of P.V.C. 35 per cent.

Example 31

0068226g xylene was heated to 90^oC. 74g methyl methacrylate was mixed with 37g methyl acrylate, 148g of a 50 per cent by weight solution of tributyltin methacrylate in xylene and 15g AIBN and the mixture was added to the hot xylene over 1 hour to produce a 36.7 per cent by volume solution of a copolymer having the same weight ratio of monomers as that of Example 30 but a lower molecular weight. 170.5g of this copolymer solution was mixed with 66g zinc oxide, 69.5g cuprous oxide, 2g Aerosil colloidal silica, 3.5g bentonite, and 1.5g n-butanol to produce a paint of P.V.C. 36.5 per cent.

Examples 32 - 33

0069Using the procedure of Example 30 copolymer solutions were produced from the following monomers: <tables id="tabl0003" num="0003"><img file="EP0051930A2_D0003.tif" /></tables>

0070Paints of P.V.C. 35 per cent were prepared from each of these copolymer solutions using the same pigment and other ingredients as in Example 30.

Example 34

007168g methyl methacrylate, 34g methyl acrylate and 68g tributyltin methacrylate were copolymerised in 300g xylene at 80°C for three hours using 5g AIBN catalyst and 25g dodecyl mercaptan chain transfer agent to produce a 37.7 per cent by volume solution of a copolymer having the same monomer weight ratio as that of Example 30 but with a lower molecular weight. 164.5g of this copolymer solution was mixed with 132g zinc oxide, 2g Aerosil colloidal silica, 3.5g bentonite, 1.3g n-butanol and 3g xylene to produce a paint of P.V.C. 35 per cent.

Example 35

0072104g ethyl acrylate, 42g methyl methacrylate and 3g methacrylic acid were dispersed in 426g water with 12g of a 10 per cent by weight aqueous solution of ammonium persulphate, 12g of a 10 per cent by weight aqueous solution of sodium metabisulphate and 4g of a 0.1 per cent by weight aqueous solution of ferrous sulphate using 5g sodium lauryl sulphate. The emulsion was heated to 30°C to induce the exothermic polymerisation reaction and then held at 80°C for fifteen minutes before cooling to 25°C. A mixture of the same quantities of monomers, initiator system and surfactant as used above was then added and the reaction mixture was held at 80°C for one hour to produce a 38.5 per cent by volume emulsion of a 70:28:2 by weight copolymer of ethyl acrylate:methyl methacrylate:methacrylic acid.

007364.2g water was mixed with 4.7g 'Calgon PT' sequestering agent, -19.2g 'Synperonic N' wetting agent, 5g Aerosil colloidal silica, 4g 'Bezaloid 677' defoamer and 31.4g of a 5 per cent by volume aqueous dispersion of a thixotropic agent. 250.5g cuprous oxide and 236.7g zinc oxide were dispersed in the aqueous mixture and 374.5g of the copolymer emulsion was added followed by 50g ethylene glycol to produce an emulsion paint of P.V.C. 31.5 per cent.

Example 36

0074A paint was prepared from the emulsion copolymer of Example 35 using the same procedure except that 16.4g of the thixotropic agent dispersion was used to replace l6.4g of the water and the pigments used were 375.8g cuprous oxide and 118.4g zinc oxide.

0075The paints of Examples 12 to 36 were tested in the rotating disc apparatus of Figures 7A and 7B of British Patent 1,457,590. In these tests the stripes of paints according to Examples 12 to 36 were applied more thickly (for example at 100 micron dry film thickness) than in the tests on the paints of Examples 1 to 11 and the average thickness of the paint film in each stripe was measured before and after 2 or 4 weeks' rotation in seawater. In each case the rate of dissolution of the paint under test was compared to the rate of dissolution of a commercially successful self-polishing paint (paint X of Examples 1 to 11). This paint has a dissolution rate in service (for example on a tanker trading between the Middle East and Northern Europe) of 8 microns per month. The results obtained are shown in Table 1. <tables id="tabl0004" num="0004"><img file="EP0051930A2_D0004.tif" /></tables>

0076All the paints under test dissolved smoothly rather than flaking in a way which would increase the roughness of the paint. Most of the paints dissolved at about the same rate as paint X or somewhat slower indicating that they had a rate of dissolution compatible with both economic use of paint and release of sufficient biocide. The paints of Examples 12, 17, 20 and 34 dissolved somewhat faster than would be desired in commercial practice but could be retarded by the addition of a minor amount of an organic hydrophobic retarder.

0077The paints of Examples 12 to 26 were tested for anti- fouling activity by applying each of them to a plaque over a vinyl resin/tar anti-corrosive paint, mounting the plaques on a panel and immersing the panel from a raft in the river Yealm estuary off Southern England between May and September. Each panel also included plaques coated with a non-toxic control (which became heavily fouled with seaweed and some animal life within 4 weeks), three conventional copper based antifouling paints A, B and C and a tin copolymer paint D pigmented with cuprous oxide. Paint A was based on a calcium zinc tall oil fatty acid salt and contained 10 per cent by weight cuprous oxide. Paint B was similar but contained some rosin binder and 24 per cent by weight cuprous oxide. Paint C was a 2-pack chlorinated rubber antifouling paint containing 41 per cent by weight cuprous oxide and 3 per cent tributyltin oxide. The antifouling performance of the paints under test is shown in Table 2.

0078The degree of fouling is rated as follows:- <ul id="ul0001" list-style="none"><li>0 - no fouling or algal slime</li><li>+ - no weed or animal fouling but some algal slime</li><li>++ - no weed or animal fouling but considerable adherent slime</li><li>+++ - small patches of stunted weed fouling</li><li>++++ - considerable fouling by stunted weed</li><li>+++++ - heavy fouling by weed and/or animal</li></ul>

0079<tables id="tabl0005" num="0005"><img file="EP0051930A2_D0005.tif" /></tables>Comparison paints A and B started to show fouling by weed within 8 weeks.