PROCESS FOR CLEANING PAINT RESIDUES FROM SURFACES

Abstract: The removal of dried paint residues from difficultly accessible surfaces is substantially speeded up by using particulate solids, which are insoluble in conventional liquid solvent-swellant compositions for removing paint residues but are soluble in water, in the form of a slurry of the particulate solids in a conventional liquid cleaner composition for paint residues, contacting the paint residues with the slurry while it is maintained in turbulent motion, removing the slurry, and rinsing with water, so as to dissolve any remaining solids from the slurry that might later contaminate the cleaned surface.

Description: Description PROCESS FOR CLEANING PAINT RESIDUES FROM SURFACES BACKGROUND OF THE INVENTION Field ofthe Invention This invention relates to an improvement in processes for cleaning totally or par¬ tially dried residues of paints and like materials from surfaces, particularly surfaces that are not readily accessible to access by conventional cleaning tools such as scrapers, abrasive bodies, and the like. More particularly, this invention relates to cleaning of pipework and similar structures that convey liquid paints and like materials to apparatus by which the paint is applied to form a protective and decorative coating on manufac¬ tured objects such as automobile bodies and appliance cabinets. Normally in such manu- facturing operations, at least the color and sometimes more fundamental characteristics ofthe protective and decorative coatings applied from the same apparatus are varied from time to time. Whenever such a change is made, it is necessary to clean the liquid paint convey¬ ing structures in order to prevent inconsistent product appearances resulting from con- tamination of one type of paint by another. Cleaning would be relatively easy if it could be assured that any unused protective coating forming liquid product would remain liquid in all parts of the conveying apparatus throughout all uses of the apparatus, including changing from one color or type of protective coating to another. However, as is well known to those skilled in the art, such a condition rarely if ever is observed in practice, and it is therefore necessary to have a process of cleaning that can satisfactorily clean surfaces on which protective coating forming liquids have been partially or totally dried. This general field will be denoted briefly hereinafter as "paint line cleaning", but it is to be understood that the invention applies to cleaning any type of surface on which an un¬ wanted and at least partially solid coating has formed as a result of contact with a liquid composition intended to form a protective solid coating on other surfaces. Discussion of Related Art Traditionally, paint line cleaning has been accomplished primarily by contacting an at least partially solid coating to be removed with a liquid solvent or swelling agent for the solid protective coating. Such a process is fully satisfactory only in the relatively few cases in which the protective coating is readily soluble in some reasonably priced solvent. Some highly effective and frequently used protective coatings, however, are chemically cross-linked to varying degrees, and usually no true solvent at all is known for densely cross-linked solids. Organic solids ofthe types used for most paints or like protective coatings, whether crosslinked or not and even if insoluble in any known liquid, can usually be swollen by some liquids, despite their lack of true solubility, and the swol¬ len solids are mechanically weaker and therefore more readily removable by mechanical action. However, obtaining effective mechanical action in the interior of a long narrow pipe remains a difficult problem. One previously attempted solution is to incorporate conventional abrasive particles into a slurry in a suitable swellant/solvent for the dried paint residues to be removed and then pump this slurry through the pipe to be cleaned. This method does improve the removal of paint but introduces a new problem: Conven¬ tional abrasive particles themselves are difficult to remove completely from a paint line, and they are extremely undesirable contaminants in liquid coating forming compositions intended to produce most decorative surfaces, because they often cause readily visible surface irregularities even when relatively small. DESCRIPTION OF THE INVENTION Objects ofthe Invention A major object ofthe invention is to provide an improved process for cleaning at least partially dried paint residues from metallic surfaces to which they are adherent, a process which will eliminate or at least reduce the above noted deficiencies of prior art procedures, especially in paint line cleaning. Another concurrent or alternative object is to provide a novel slurry of water soluble particulate solids in a nonaqueous liquid that is effective for swelling and/or dissolving paint residues. Other objects will be apparent from the description below. General Principles of Description Except in the claims and the specific examples, or where otherwise expressly in¬ dicated, all numerical quantities in this description indicating amounts of material or con¬ ditions of reaction and/or use are to be understood as modified by the word "about" in describing the broadest scope ofthe invention. Practice within the numerical limits stat¬ ed is generally preferred, however. Also, unless expressly stated to the contrary: percent, "parts of, and ratio values are by weight; the term "polymer" includes "oligomer", "co- polymer", "terpolymer", and the like; the first definition or description of the meaning of a word, phrase, acronym, abbreviation or the like applies to all subsequent uses ofthe same word, phrase, acronym, abbreviation or the like and applies, mutatis mutandis, to normal grammatical variations thereof; the description of a group or class of materials as suitable or preferred for a given purpose in connection with the invention implies that mixtures of any two or more ofthe members ofthe group or class are equally suitable or preferred; specification of materials in ionic form implies the presence of sufficient coun¬ terions to produce electrical neutrality for the composition as a whole; and any counter¬ ions thus implicitly specified preferably are selected from among other constituents ex- plicitly specified in ionic form, to the extent possible; otherwise such counterions may be freely selected, except for avoiding counterions that act adversely to the objects ofthe invention. Summary ofthe Invention It has been discovered that suspended solid particles other than conventional abrasives are also effective in assisting the removal of paint residues from metal surfaces to which they adhere. This permits a substantial improvement in the reliability and/or the speed of elimination of all contamination from paint lines and other surfaces bearing residues of paint to be removed, by selecting a solid that is substantially insoluble in a suitable swellant/solvent liquid composition used to remove paint residues but is readily soluble in a second liquid that can be pumped through the paint line, or otherwise con¬ tacted with some other type of surface cleaned from paint residues formerly present thereon, after at least most of the first swellant/solvent liquid has been removed from contact with the cleaned surface. A process according to the invention correspondingly comprises, or preferably consists essentially of, removing at least partially dried paint residues from a surface bearing a coating of such paint residues by steps of: (I) providing a first liquid that is a swellant/solvent for the paint residues to be re¬ moved, a second liquid that is chemically distinct from the first liquid, and partic¬ ulate solids that are substantially insoluble in the first liquid but substantially sol- uble in the second liquid; (II) forming a slurry ofthe particulate solids in the first liquid; (III) causing the slurry formed in step (II) to move in turbulent flow and to contact the surface bearing a coating of paint residues to be removed while the slurry is mov¬ ing in turbulent flow, contact between the slurry moving in turbulent flow and the surface bearing a coating of paint residues to be removed being maintained until a desired degree of removal of paint residues from the surface bearing a coating of paint residues to be removed has been achieved, so that the former surface bearing a coating of paint residues to be removed has been changed to a cleaned surface; (TV) after step (III), discontinuing contact between the cleaned surface and the slurry ofthe particulate solid in the first liquid; and (V) after step (TV), contacting the cleaned surface with the second liquid in a suffi¬ cient volume having sufficiently rapid motion for a sufficient time to remove any residue ofthe particulate solids from the cleaned surface by dissolving the resi¬ due ofthe particulate solids in the second liquid. A suspension according to the invention comprises, preferably consists essentially of, or more preferably consists of, a dispersed particulate solid phase and a continuous liquid phase, the particulate solid being substantially insoluble in the continuous liquid phase but substantially soluble in water. Brief Description ofthe Drawing Figure 1, the sole drawing figure, is a schematic diagram of laboratory apparatus used to test and demonstrate the operation ofthe invention. Detailed Description ofthe Invention. Including Preferred Embodiments Whenever herein any liquid or solid material is described as "substantially insolu¬ ble" in a chemically distinct liquid material, the solubility at 25 °C ofthe first mentioned liquid or solid material in the chemically distinct liquid material preferably is, with in- creasing preference in the order given, not more than 10, 5, 2, 1, 0.5, 0.3, 0.2, 0.1, 0.05, 0.03, 0.02, 0.01, 0.005, 0.003, 0.002, 0.001, 0.0005, 0.0003, or 0.0002 grams per liter (hereinafter usually abbreviated as "g/L") ofthe chemically distinct liquid material; and, independently, whenever herein any liquid or solid material is described as "substantially soluble" in a chemically distinct liquid material, the solubility at 25 °C ofthe first men- tioned liquid or solid material in the chemically distinct liquid material preferably is, with increasing preference in the order given, at least 15, 20, 25, 30, 35, 40, 45, 50, 55, 60, 65, 70, 75, 80, 85, 90, 95, or 100 g/L. An optional and often preferred process step that may be used without changing the essential character ofthe invention is contacting the cleaned surface formed in step (IV) with a third liquid having the properties that (i) the first liquid is substantially solu¬ ble in it and (ii) the third liquid is substantially soluble in the second liquid, this contact- ing occurring before step (V) as described above. Inasmuch as the first liquid often is not substantially soluble in the second liquid, such use of a third intermediate liquid guards against the danger that would otherwise exist of some pockets of first liquid being re¬ tained in crevices or other irregularities ofthe cleaned surface. Such retention is particu¬ larly likely in complex pipework involving many bends, distributors, variations in diam- eter over a relatively short distance, and/or the like often found in practical use where complex shaped objects are to be painted. If necessary or desired, still more additional intermediate liquids could be used, but this has not been found advantageous normally. The third liquid when used can and often preferably does also contain some particulate solid to aid in further removal of paint residues. For convenience and economy, it is normally preferred that most or all ofthe se¬ cond liquid as described above consist of water. It is normally preferred, if the fastest possible cleaning of paint residues is desired, that the first liquid as described above con¬ sist of the same liquid chemical substance(s) as are normally used now in paint line cleaning for removing the same type of paint residues as are to be removed in a process according to this invention. However, where economy of material consumption is more important than speed, it is possible with this invention to use somewhat inferior swellant/ solvent liquids that might not remove paint at a practically useful rate in the absence of dispersed solids; such swellant/solvent liquids are often substantially less expensive than the swellant solvent liquids normally used in the absence of any dispersed solids as de- scribed herein. For most types of conventional paints and like materials, the residues from which are to be removed from metallic or other hard surfaces, the first liquid preferably com¬ prises, with increasing preference in the order given, at least 35, 45, 50, 55, 60, or 65 % of materials selected from the group consisting of aromatic and terpene hydrocarbons, esters, alcohols, ketones, amides, halocarbons, and halohydrocarbons. More preferably, these materials are selected from the group consisting of: (i) aromatic and teφene hydro¬ carbons; (ii) lactams containing at least five carbon atoms, (iii) ether alcohols, and (iv) halocarbons and halohydrocarbons containing at least two halogen atoms per molecule. Still more preferably, any ether alcohols used contain no more than 10 carbon atoms and one hydroxyl group per molecule, and, independently, any halohydrocarbons used con¬ tain not more than, with increasing preference in the order given, 6, 5, 4, 3, 2, or 1 carbon 5 atom(s) and at least two atoms selected from the group consisting of chlorine and fluor¬ ine. For removing most types of conventional paints and like materials, a combination of aromatic hydrocarbons and lactams containing at least five carbon atoms is preferred for the first liquid even more than either ofthese components ofthe combination alone. o The ratio of the amount of lactam to the amount of aromatic hydrocarbon preferably is at least, with increasing preference in the order given, 1.0: 1.0, 1.5 : 1.0, 1.8 : 1.0, 2.1 : 1.0, 2.4:1.0, or 2.6:1.0 and independently preferably is not more than, with increasing prefer¬ ence in the order given, 10: 1.0, 8: 1.0, 6: 1.0, 4.0: 1.0, 3.5: 1.0, 3.2: 1.0, 2.9: 1.0, or 2.7: 1.0. When these preferred first and second liquids are used, a third intermediate liquid 5 as described above is preferably used and when used is preferably selected from the group consisting of alcohols, ketones, and aldehydes, all independently preferably having a ratio ofthe number of carbon atoms in each molecule to the number of oxygen atoms in a hydroxy, ketone, or aldehyde moiety in each molecule that is not more than 4, or more preferably not more than 3. The single most preferred third liquid is isopropyl al- 0 cohol. The particulate solids required according to this invention may be selected from a wide variety of chemical substances, as long as the solubility criteria specified herein are satisfied and the substance(s) used have no adverse effect on the properties of the cleaned surface. For example, alkali metal and ammonium borates, carbonates, chlor- 5 ides, chlorates, nitrates, phosphates (including condensed phosphates), silicates, and sul¬ fates, all including partially hydrogen retaining anions and solid hydrates where chemic¬ ally possible, along with most other inorganic nitrates and most metal acetates and for¬ mates, and even some highly polar purely organic neutral compounds such as sugar, are suitable particulate solids for use with most types of first liquids when water is the sec- 0 ond liquid in a process according to the invention. Generally, the basis of preferences among these materials is economic: whatever material with suitable solubility character¬ istics is available in desirable particle size grades at a low price would normally be pre- ferred for the particulate solids. Sodium hydrogen carbonate has been found to be readily available in a preferred size grade and very well suited to use as the particulate solids ac¬ cording to this invention. There are no narrow limitations on the size ofthe particles in the particulate solid required according to this invention. However, it is preferred that the particle size be small enough that most ofthe particles can be readily suspended in the moving slurry of the particulate solid in the first liquid that is required in part of a process according to this invention, but also large enough to transfer a useful amount of momentum to the surface bearing a coating of paint residues to be removed when the suspended solid particles col- lide with paint residues to be removed. For materials with the density of sodium hydro¬ gen carbonate (i.e., 2.2 grams per cubic centimeter), the preferred particle sizes are small enough that they may conveniently be measured by sieving. Specifically, it is preferred that for any representative sample ofthe particulate solid, not more than, with increasing preference in the order given, 10, 8, 6, 4, 3, 2.0, or 1.5 % ofthe sample be retained on a standard 35 mesh screen (this and all other mesh sizes stated herein being according to U. S. standards) and independently preferred that not more than, with increasing prefer¬ ence in the order given, 10, 8, 6, 4, 3, 2.0, or 1.5 % of the sample pass through a 200 mesh screen. Independently, it is preferable that at least, with increasing preference in the order given, 10, 20, 25, 30, 33, 36, or 39 % ofthe particulate solid be retained on a 50 mesh screen but independently that no more than, with increasing preference in the order given, 70, 60, 50, 47, 45, 43, or 41 % ofthe particulate solid be retained on a 50 mesh screen. Also, independently, it is preferred that at least, with increasing preference in the order given, 70, 75, 80, 85, 90, 92, 94, 95, 96, or 97 % ofthe particulate solid be retained on a 100 mesh screen. There are no narrow limits on the proportion between the particulate solid and the amount ofthe first liquid or third liquid in which the particulate solid is slurried during a process according to this invention. However, there are preferable values, because too little of the particulate solid will make any benefit of the invention difficult to detect, while too much ofthe particulate solid will increase the effective viscosity ofthe slurry and thereby reduce the turbulence for a constant speed of motion of the slurry. For a par¬ ticulate solid with the density of sodium hydrogen carbonate, the concentration of partic¬ ulate solid per unit volume of first (or third) liquid as described above preferably is, with increasing preference in the order given, at least 5, 10, 15, 20, or 22 g/L of liquid and in¬ dependently preferably is, with increasing preference in the order given, not more than 300, 150, 100, 80, 65, 50, 45, 42, 40, or 38 g/L. If the density ofthe particulate solid is substantially different from that of sodium hydrogen carbonate, the values given above should be adjusted to result in the same volume percent of particulate solids to liquid in which the particulate solids are slurried as would result from the above specified con¬ centrations, for sodium hydrogen carbonate. Independently of other preferences, in order to promote facile suspension ofthe particulate solids in the first (or third) liquid as described above, the difference in density between the particulate solids and the liquid in which they are slurried preferably should not be greater than, with increasing preference in the order given, 5, 4, 3.5, 3.0, 2.8, 2.6, 2.4, 2.2, 2.0, 1.8, 1.6, 1.4, 1.2, 1.0, 0.8, 0.6, 0.4, or 0.2 g/L. In order to obtain substantial advantages from the use of this invention, the partic¬ ulate solids suspended in the first liquid must be propelled with substantial force against the paint residues on a surface bearing a coating of paint residues to be removed. This is most readily accomplished by moving the suspension of the particulate solids in the first liquid rapidly enough to maintain turbulent flow. The degree of turbulence is com¬ monly measured by a "Reynolds number", N Re , defined by the following equation: N Re = L»V»p/μ, where L represents a characteristic linear dimension, which for flow in a circular pipe is the diameter ofthe pipe and for other kinds of flow can be determined as known in the art; V represents the fluid flow velocity; p represents the density ofthe flu¬ id, and μ represents the viscosity of the fluid. All these parameters except N Re itself should be expressed in mutually consistent dimensions, so that N Re is dimensionless. With increasing preference in the order given, motion of the suspension of particulate solids in the first liquid during step (III) of a process according to this invention as de¬ fined above, and in any intermediate liquid in which particulate solids are suspended, is sufficiently rapid that the corresponding Reynolds number is at least, with increasing preference in the order given, 2000, 3000, 5000, 7000, 9000, 11,000, 13,000, 15,000, 17,000, 18,000, 19,000, or 20,000. For the sake of economy and other practical benefits, a process according to the invention normally is conducted within a container in which rapidly moving liquids and slurries of solids in liquids can be brought into contact with the paint residues to be re- moved, without loss of such liquids and slurries through or over the walls ofthe contain¬ er. For the most preferred use, paint line cleaning, the paint line itself serves as such a container. If the surface bearing a coating of paint residues to be removed is not itself part of an interior wall of a container, a separate container into which the surface bearing a coating of paint residues to be removed will fit and can be covered completely with moving liquids and slurries of solids in liquids, without loss of such liquids and slurries through or over the walls ofthe container, is normally preferred and can be readily ac¬ complished by means known in the art. The invention and its benefits may be further appreciated from consideration of the following working examples and comparison examples. Test Apparatus The test apparatus used in most of the examples and comparison examples is shown schematically in Figure 1, the sole drawing figure, wherein reference number 1 indicates an open-top reservoir in which a liquid or suspension can be stored when not in use, and from which a pump inlet pipe 2 leads to a pump 3. When powered by con¬ ventional means not shown, the pump discharges fluid through pump outlet tube 4, which is connected to test section 6 via conventional tubing to pipe couplings 5 and 5'. When in use, fluid flows from the test section 6 through reservoir delivery tube 8 back to reser¬ voir 1, which is open at the top but has sufficiently high walls to contain the volume of liquid in the apparatus. Valve 7 enables control of flow. Reservoir 1 and pipe 2 are con¬ structed from galvanized steel pipe, with a diameter of about 10 centimeters for the main body ofthe reservoir and about 19 mm for pipe 2, with a conventional reducer between them. The pump acts as a valve when not powered, so that fluid can be added to the reservoir without being lost, and the height ofthe reservoir above the pump inlet helps prime the pump when the pump is turned on. Tubes 4 and 8 are all constructed of stain¬ less steel tubing with a diameter of about 1 centimeter, while test section 6 was normally constructed of cylindrical glass pipe with an inside diameter of 1.6 centimeters. General Test Method In use, the liquid or slurry to be evaluated was placed in reservoir 1 ofthe test ap- paratus. A glass tube with paint residues pre-dried thereon was placed in the apparatus as test section 6. Pump 3 was turned on, so as to cause a flow ofthe tested liquid or slur¬ ry from the bottom ofthe reservoir through the test section and back to the top ofthe res- ervoir, at a rate of 19 liters per minute, corresponding to a Reynolds number of about 25,000 in test section 6 when the liquid pumped through is water and the amount of sol¬ ids present is not so large that it substantially increases the density or viscosity ofthe sus¬ pension compared to that ofthe liquid continuous phase ofthe suspension. The paint residues to be tested were put into place on the inside of a glass pipe test section by stoppering one end of the test section, filling the stoppered pipe with paint, inverting it and allowing the paint to drain, and then drying the residue that re¬ mained on the walls by exposure to ambient air for at least four days. Specific Tests - Group 1 1.1. A test section was coated with Du Pont water-borne base coat 521R95047. The coated test section was put into place in the apparatus as described above and the reser¬ voir initially loaded with P3® Paint Line Cleaner 118, commercially supplied by the Par¬ ker Amchem Division of Henkel Corp., Madison Heights, Michigan, USA. P3® Paint Line Cleaner 118 is a conventional high quality paint line cleaner in which the two major ingredients are N-methyl pyrrolidone and light aromatic naptha petroleum distillate. The liquid paint line cleaner was then circulated for 15 minutes without completely cleaning the tube. After this time, a sufficient amount of Annax™ Maintenance XL Formula partic¬ ulate sodium hydrogen carbonate, commercially supplied by Church & Dwight, to pro- vide a concentration of 30 g/L of particulate solids in the volume of liquid in the apparat¬ us was added. The supply of sodium hydrogen carbonate used had a particle size distri¬ bution determined by sieving as shown in Table 1 below. After addition ofthe particu¬ late sodium hydrogen carbonate solids, pumping was continued, and substantial addition¬ al paint removal was achieved. The slurry was then removed from the apparatus and the parts of the apparatus cleaned and blown dry with air. Isopropyl alcohol (hereinafter usually abbreviated as "IPA") was then substituted for the cleaning slurry in the residue and circulated through the system for 5 minutes. This in turn was then drained and replaced by tap water, with an initial pH value of 7.45. After the first volume of water had circulated for 5 minutes, its pH value had risen to 8.89, indicative of the water having dissolved some residual sodium hydrogen carbonate. The water was then drained from the system, and a second increment of water ofthe same size as the first was added and again circulated by the TABLE 1 Screen Mesh Size Percent Retained on Screen Percent Passing Through Screen 6 0.00 100.00 8 0.00 100.00 14 0.00 100.00 25 0.00 100.00 35 1.30 98.70 50 39.02 60.98 100 57.46 3.52 150 1.52 2.25 200 0.95 1.30 325 0.67 0.63 Pan 0.63 — The four liquid charges to the apparatus were also examined. The first looked like somewhat thinned paint, except for a noticeable amount of retained particulate sol¬ ids. The second liquid (IPA) was substantially clear and transparent in its liquid portions, but had dispersed, readily settling, grey residue, believed to be derived from the paint res¬ idues, and some dispersed sodium hydrogen carbonate. The third liquid charge, original¬ ly tap water, was slightly cloudy with grey residue, while the fourth liquid charge, the second increment of tap water, was almost completely clear. 1.2. This test was performed in the same manner as 1.1 , except that: (i) the initial per¬ iod of circulation with liquid paint line cleaner only was 45 minutes; (ii) when this paint line cleaner was removed, it was replaced with sodium hydrogen carbonate and IPA, not with more paint line cleaner, and the concentration of particulate solids was 38 g/L; the dispersion in IPA was circulated for 40 minutes total, with rotation of the test section after the first 25 minutes; the initial liquid had no suspended sodium hydrogen carbonate (because none had been present in it); the IPA had considerably more suspended sodium hydrogen carbonate; the first increment of water had a pH of 8.43 after 15 minutes circu¬ lation, and the second increment of water had a pH of 7.9 after 15 minutes circulation. 1.3. This test was the same as 1.1 , except that: the initial period of circulation of the 118 Paint Line Cleaner was only 5 minutes, and substantially none of the tube surface was cleared of all paint residues; the amount of sodium hydrogen carbonate particulate solids added gave a concentration of 38 g/L in suspension, and after the first five minutes of use of this slurry, there was considerably more evidence of paint removal than without the particulate solids in the same time; the circulation ofthe slurry was continued for 7.7 hours, with the test section rotated after 2 hours, rotated again after another 1 hour, addi¬ tional particulate sodium hydrogen carbonate solids, sufficient to give a concentration of 76 g/L, added and the test section rotated again after 2 more hours, and the test section rotated again after 1 more hour; and the tube was completely cleaned except for narrow streaks near the ends and in a center section that appeared to have low turbulence, judged by visual examination ofthe flow after most ofthe wall ofthe test section had become clear enough to allow observation through the walls ofthe motion ofthe suspended sol¬ ids. 1.4. (Comparative example only) This was substantially the same as 1.1 , except that: No particulate solids and no other liquids than the 118 Paint Cleaner were ever added; the test section was rotated after two hours; and the degree of removal was about 40 % after one hour, 50 % after 3 hours, and 70 % after 5 hours total; however, all portions of the test section retained at least spotty paint residues, with no large area ofthe test sec- tion completely clean, as had been achieved in a shorter time with the use of suspended solids. Group 2 In the same general manner as described for Group 1, the following particulate solids are used: ammonium borate, ammonium carbonate, ammonium sulfate and hydro- gen sulfate, potassium borates and hydrogen borates, potassium carbonate and hydrogen carbonate, potassium nitrate, potassium orthophosphate and hydrogen orthophosphates, potassium silicates and hydrogen silicates, potassium sulfate and hydrogen sulfate, sodi¬ um borates and hydrogen borates, sodium carbonate and hydrogen carbonate, sodium ni¬ trate, sodium orthophosphate and hydrogen orthophosphates, sodium silicates and hydro- gen silicates, and sodium sulfate and hydrogen sulfate.

Claims: The invention claimed is: 1. A process for removing at least partially dried paint residues from a surface bear¬ ing a coating of such paint residues, said process comprising steps of: (I) providing a first liquid that is a swellant/solvent for the paint residues to be re- moved, a second liquid that is chemically distinct from the first liquid, and partic¬ ulate solids that are substantially insoluble in the first liquid but substantially sol¬ uble in the second liquid; (II) forming a slurry ofthe particulate solids in the first liquid; (III) causing the sluπy formed in step (II) to move in turbulent flow and to contact the surface bearing a coating of paint residues to be removed while the slurry is mov¬ ing in turbulent flow, contact between the slurry moving in turbulent flow and the surface bearing a coating of paint residues to be removed being maintained until a desired degree of removal of paint residues from the surface bearing a coating of paint residues to be removed has been achieved, so that the former surface bearing a coating of paint residues to be removed has been changed to a cleaned surface; (TV) after step (TLT), discontinuing contact between the cleaned surface and the slurry ofthe particulate solid in the first liquid; and (V) after step (TV), contacting the cleaned surface with the second liquid in a suffi- cient volume having sufficiently rapid motion for a sufficient time to remove any residue ofthe particulate solids from the cleaned surface by dissolving such resi¬ due ofthe particulate solids in the second liquid. 2. A process according to claim 1 , comprising, between steps (TV) and (V), addition¬ al steps of: (IV') contacting the cleaned surface from the end of step (TV) with a third liquid that is chemically distinct from both said first and said second liquids, said third li¬ quid having the properties that (i) said first liquid is substantially soluble in it and (ii) it is substantially soluble in said second liquid, said third liquid optionally in¬ cluding substantially insoluble solids suspended therein, any such solids being substantially soluble in said second liquid; and (IV") discontinuing contact between the cleaned surface and said third liquid. 3. A process according to claim 2, wherein the turbulent flow of the slurry of partic¬ ulate solids in the first liquid during step (III) coπesponds to a Reynolds number of at least about 5000. 4. A process according to claim 1, wherein the turbulent flow ofthe slurry of partic- ulate solids in the first liquid during step (TTT) coπesponds to a Reynolds number of at least about 3000. 5. A process according to any of claims 1 through 4, wherein: at least 35 % ofthe first liquid is selected from the group consisting of aromatic and teφene hydrocarbons, esters, alcohols, ketones, amides, halocarbons, and halohydrocarbons; the particulate solids provided in step (I) have particle sizes such that not more than about 10 % of a representative sample ofthe particulate solids will be retained on a 35 mesh screen, not more than about 10 % of said sample will pass through a 200 mesh screen, from about 10 to about 70 % of said sample will be retained on a 50 mesh screen, and at least about 70 % of said sample will be retained on a 100 mesh screen; the volume percent of partic- ulate solids in the slurry contacted during step (ST) with the surface to be cleaned is with¬ in a range of volume percent conesponding to from 5 to 150 g/L of sodium hydrogen car¬ bonate in the same first liquid as is used to form the slurry contacted during step (III) with the surface to be cleaned; the difference in density between the particulate solids and the first liquid provided in step (I) is not more than about 3.5 g/L; the turbulent flow of the slurry of particulate solids in the first liquid during step (III) coπesponds to a Reynolds number of at least about 7000; and the second liquid is predominantly water. 6. A process according to claim 5, wherein: at least 45 % ofthe first liquid is select¬ ed from the group consisting of (i) aromatic and teφene hydrocarbons; (ii) lactams con¬ taining at least five carbon atoms, (iii) ether alcohols, and (iv) halocarbons and halohy- drocarbons containing at least two halogen atoms per molecule; the particulate solids provided in step (I) have particle sizes such that not more than about 6 % of a rep¬ resentative sample of the particulate solids will be retained on a 35 mesh screen, not more than about 6 % of said sample will pass through a 200 mesh screen, from about 20 to about 60 % of said sample will be retained on a 50 mesh screen, and at least about 75 % of said sample will be retained on a 100 mesh screen; the volume percent of particulate solids in the slurry contacted during step (III) with the surface to be cleaned is within a range of volume percent coπesponding to from 10 to 100 g/L of sodium hydrogen car¬ bonate in the same first liquid as is used to form the slurry contacted during step (HI) with the surface to be cleaned; the difference in density between the particulate solids and the first liquid provided in step (I) is not more than about 2.8 g/L; and the turbulent flow ofthe sluπy of particulate solids in the first liquid during step (TTT) coπesponds to a Reynolds number of at least about 9000. 7. A process according to claim 6, wherein: at least 55 % of the first liquid is select¬ ed from the group consisting of (i) aromatic and teφene hydrocarbons; (ii) lactams con¬ taining at least five carbon atoms, (iii) ether alcohols that contain no more than 10 carbon atoms and one hydroxyl group per molecule, and (iv) halocarbons and halohydrocarbons containing not more than 3 carbon atoms and at least two atoms selected from the group consisting of chlorine and fluorine per molecule; the particulate solids provided in step (I) have particle sizes such that not more than about 6 % of a representative sample ofthe particulate solids will be retained on a 35 mesh screen, not more than about 6 % of said sample will pass through a 200 mesh screen, from about 20 to about 60 % of said sample will be retained on a 50 mesh screen, and at least about 75 % of said sample will be re¬ tained on a 100 mesh screen; the volume percent of particulate solids in the slurry con¬ tacted during step (DI) with the surface to be cleaned is within a range of volume percent corresponding to from 10 to 100 g/L of sodium hydrogen carbonate in the same first liquid as is used to form the slurry contacted during step (TTT) with the surface to be cleaned; the difference in density between the particulate solids and the first liquid pro¬ vided in step (I) is not more than about 2.8 g/L; and the turbulent flow ofthe sluπy of particulate solids in the first liquid during step (III) coπesponds to a Reynolds number of at least about 9000. 8. A process according to claim 7, wherein: at least 60 % of the first liquid is select¬ ed from the group consisting of (i) aromatic hydrocarbons and (ii) lactams containing at least five carbon atoms; the particulate solids provided in step (I) have particle sizes such that not more than about 4 % of a representative sample ofthe particulate solids will be retained on a 35 mesh screen, not more than about 4 % of said sample will pass through a 200 mesh screen, from about 25 to about 50 % of said sample will be retained on a 50 mesh screen, and at least about 80 % of said sample will be retained on a 100 mesh screen; the volume percent of particulate solids in the slurry contacted during step (III) with the surface to be cleaned is within a range of volume percent coπesponding to from 15 to 65 g/L of sodium hydrogen carbonate in the same first liquid as is used to form the slurry contacted during step (DI) with the surface to be cleaned; the difference in density 5 between the particulate solids and the first liquid provided in step (I) is not more than about 2.4 g/L; and the turbulent flow ofthe slurry of particulate solids in the first liquid during step (III) corresponds to a Reynolds number of at least about 11,000. 9. A process according to claim 8, wherein: at least 65 % ofthe first liquid is select¬ ed from the group consisting of (i) aromatic hydrocarbons and (ii) lactams containing at o least five carbon atoms and contains both of these types of solvents in a ratio of lactams to hydrocarbons in a range from 1.8: 1.0 to 4.0: 1.0; the particulate solids provided in step (I) have particle sizes such that not more than about 2.0 % of a representative sample of the particulate solids will be retained on a 35 mesh screen, not more than about 2.0 % of said sample will pass through a 200 mesh screen, from about 30 to about 45 % of said 5 sample will be retained on a 50 mesh screen, and at least about 90 % of said sample will be retained on a 100 mesh screen; the volume percent of particulate solids in the slurry contacted during step (Ifl) with the surface to be cleaned is within a range of volume percent coπesponding to from 20 to 45 g/L of sodium hydrogen carbonate in the same first liquid as is used to form the slurry contacted during step (III) with the surface to be 0 cleaned; the difference in density between the particulate solids and the first liquid pro¬ vided in step (I) is not more than about 2.0 g/L; and the turbulent flow ofthe slurry of particulate solids in the first liquid during step (III) coπesponds to a Reynolds number of at least about 13,000. 10. A process according to claim 9, wherein: the ratio of lactams to hydrocarbons is 5 in a range from 2.4: 1.0 to 3.2: 1.0; the particulate solids provided in step (I) have particle sizes such that not more than about 1.5 % of a representative sample ofthe particulate solids will be retained on a 35 mesh screen, not more than about 1.5 % of said sample will pass through a 200 mesh screen, from about 36 to about 45 % of said sample will be retained on a 50 mesh screen, and at least about 95 % of said sample will be retained on 0 a 100 mesh screen; the volume percent of particulate solids in the slurry contacted during step (III) with the surface to be cleaned is within a range of volume percent cor- responding to from 20 to 38 g/L of sodium hydrogen carbonate in the same first liquid as is used to form the slurry contacted during step (DI) with the surface to be cleaned; the difference in density between the particulate solids and the first liquid provided in step (I) is not more than about 1.4 g/L; and the turbulent flow ofthe slurry of particulate sol- ids in the first liquid during step (TTT) coπesponds to a Reynolds number of at least about 15,000. 11. A process according to claim 10, wherein the particulate solids are selected from the group consisting of ammonium borate, ammonium carbonate, ammonium sulfate and hydrogen sulfate, potassium borates and hydrogen borates, potassium carbonate and hy- drogen carbonates, potassium nitrate, potassium orthophosphate and hydrogen ortho¬ phosphates, potassium silicates and hydrogen silicates, potassium sulfate and hydrogen sulfate, sodium borates and hydrogen borates, sodium carbonate and hydrogen carbonate, sodium nitrate, sodium orthophosphate and hydrogen orthophosphates, sodium silicates and hydrogen silicates, and sodium sulfate and hydrogen sulfate. 12. A process according to claim 11 , where the particulate solids are sodium hydro¬ gen carbonate.

Inventors: JAREMA CHESTER P, JAREMA, CHESTER, P.
Applicants: HENKEL CORP, JAREMA CHESTER P, HENKEL CORPORATION, JAREMA, CHESTER, P.
Application year: 1996
Main classification: B08B3
IPC codes: B44D3, C09D9