GB2229453A - Forming a metal coating - Google Patents

Forming a metal coating Download PDF

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Publication number
GB2229453A
GB2229453A GB9002268A GB9002268A GB2229453A GB 2229453 A GB2229453 A GB 2229453A GB 9002268 A GB9002268 A GB 9002268A GB 9002268 A GB9002268 A GB 9002268A GB 2229453 A GB2229453 A GB 2229453A
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United Kingdom
Prior art keywords
metal
compound
reagent
paint
volatile
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
GB9002268A
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GB9002268D0 (en
Inventor
Michael Cox
Rajendra Joshi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
National Research Development Corp UK
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National Research Development Corp UK
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Filing date
Publication date
Priority claimed from GB898902312A external-priority patent/GB8902312D0/en
Priority claimed from GB898902311A external-priority patent/GB8902311D0/en
Priority claimed from GB898902310A external-priority patent/GB8902310D0/en
Application filed by National Research Development Corp UK filed Critical National Research Development Corp UK
Publication of GB9002268D0 publication Critical patent/GB9002268D0/en
Publication of GB2229453A publication Critical patent/GB2229453A/en
Withdrawn legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/02Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition
    • C23C18/08Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by thermal decomposition characterised by the deposition of metallic material
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/06Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the deposition of metallic material
    • C23C16/18Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the deposition of metallic material from metallo-organic compounds

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  • Chemical & Material Sciences (AREA)
  • Metallurgy (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemically Coating (AREA)
  • Other Surface Treatments For Metallic Materials (AREA)
  • Paints Or Removers (AREA)
  • Chemical Vapour Deposition (AREA)

Abstract

This invention relates to a method of forming a metal coating on a surface. According to one embodiment, the method comprises decomposing at the surface a fluid comprising: a first compound between a first metal and a polydentate reagent, and a second compound between a second metal and the same or another polydentate reagent the reagent(s) being volatile, whereby the metals are co-deposited on the surface. The first and/or second compounds may be volatile and the fluid may be a vapour or a liquid. The mixed metals coating may be formed by decomposition of a mixed metal complex, eg (Ni/Cu) (heptandioate)2 or alternatively the second metal is the surface in which case the second volatile compound is formed from reagent liberated by decomposition of the first volatile compound reacting with the surface, eg NiFe alloy is deposited on steel by decomposition of nickel bis 1,1,1-trifluoro-2,4-pentandioate. The decomposition is preferably affected by reduction. In another embodiment a metallic paint comprises a compound between the metal or each of the metals of the paint and a polydentate reagent, said compound(s) being dissolved in a paintable solvent. The paint is applied to an object or made up on the object by dissolving in the solvent after the object has been placed in the solvent. The solvent is allowed to evaporate and then a gaseous or volatile substance is applied to reduce the compound to release the metal. In an example particles of Fe14NdB are coated with copper by using a paint containing a copper complex of tert-butyl acetyl acetone. In addition metal powder, eg copper powder, is made by atomising this paint through an atomising nozzle and reducing.

Description

FORMING A METAL COATING This invention relates to a method of forming a single-metal or mixed-metals coating on a surface, to a metallic paint, to a method of painting and to a method of spray-forming powders using the paint.
Metallic paints are known which comprise metal (e.g. zinc or aluminium) particles suspended tn binder, pigment and volatile solvent. Such paints are easy to apply but cannot give a seamless coherent metal coating, which can be required in demanding and advanced technical applications.
According to the present invention, a metallic paint comprises a compound between the metal or each of the metals of the paint and a polydentate reagent, said compound(s) being dissolved in a paintable solvent.
An object is painted, according to the invention, by applying thereto a paint as set forth above, allowing the solvent to evaporate, and applying a gaseous or volatile substance which can decompose said compound(s) to release said metal(s). Metal powder may be made by atomising the paint and applying a said gaseous compound.
According to another aspect of the Invention, the method of forming mixed-metal coatings on a surface comprises decomposing at the surface a fluid e.g. vapour comprising: a first preferably volatile compound between a first metal and a polydentate reagent, and a second preferably volatile compound between a second metal and the same or another polydentate reagent, wherein the reagents is/are volatile, whereby the metals are co-deposited on the surface. The reagent(s) and the compounds are preferably stable in air. The decomposition preferably yields the reagent(s) directly, which accordingly may be recovered for re-use.
Transport of the 'bulk' complex in vapour phase and its reaction on the heated substrate can in certain cases result in interactions between the regenerating ligand and substrate material, i.e. removal of surface oxide, or the formation of a volatile intermediate which itself is reduced later. This would particularly be enhanced where the chelating ligands are extremely active' toward the base material. Thus, in one option, the said second metal is the surface and the said second volatile compound is formed from reagent liberated upon decomposition of the first volatile compound. By this technique, interpenetration of metals can be achieved at lower temperatures than if, say, diffusion was being relied upon.
Preferably the decomposition of the polydentate reagent(s) to metal is by reduction. Preferably the reduction is performed by a gas or gases.
Preferably the donor atoms of the said reagent(s) are any selection from N, 0 and S. Preferably the said reagent (or one of said reagents) is a Schiff base or a ss-diketone. Both these are air-stable and non-toxic, unlike for example metal alkyls and metal carbonyls.
Where the reagents are different for the two metals, at least one may comprise ballasting substituents. Thus, by exploiting the resulting differential volatilities of the two compounds, their relative vapour pressures can be varied so as to adjust the composition of the resulting metal mixture if other ways of altering the vapour composition are not available.
One of the metals may be copper and the other may be nickel.
The substrate may be a metal or glass or ceramic (e.g. alumina) or a membrane requiring to be metallised.
UK Patent GB 21359848, the disclosure of which is imported by reference, claims a method of winning metal from ore, and discloses for that purpose compounds which may find use in this invention, such as, in the case of Cu(II), tetradentate Schiff base reagents.
(3-diketones which may be used include for example 2,2,6,6 tetramethyl 3,5 heptadione (trivially called tert-butyl acetyl acetone), two molecules of which complex each copper atom:
The removal of surface oxide, mentioned earlier, takes place as follows.
Complex ML + Decomposing agent say H2 g Deposited metal M + Polydentate reagent LH2 Regenerated LH2 + Surface oxide MO + H20 vapour + ML Note that surface oxide can be removed at low temperature (e.g. 3000C), below the onset of rapid diffusion. This feature improves the adhesion of deposited metal.
The invention will now be described by way of example.
The co-deposition of metals, e.g. nickel and copper on various substrates, was carried out using physically mixed 'powdered' proportions of respective metal complexes. A range of metallic complex mixtures was prepared by physical mixing, and each mixture was shaken and volatilised prior to reduction and deposition. The volatilisation temperatures were dependent upon the 'mixtures' used, generally in the region of 180-2000C for ss-diketonoate complexes, and around 2500C for Schiff's base complexes. The relative percentage of respective metals in the deposit depends as mentioned on the relative volatilities of the complexes. Thus a mixture of nickel and copper 2,2,6,6-tetramethyl-3,5-heptandioate complexes in the proportions Ni 70:Cu 30 gave a deposit containing the same ratio of metals.
With a mixture of the same ratio, but 2,4-pentandione as the chelate, a higher proportion of copper was detected.
In the following examples, deposition temperatures of between 350 - 450 * 100C and total gas flow (carrier and reductant) of 75 s 5 cm3/min were used.
Prior to any deposition all substrates were washed in 0.1 M HC1, followed by an acetone rinse.
EXAMPLE 1: NiCu alloy is deposited on mild steel.
A physically mixed composition of Ni/Cu (heptandioate)2 complex mentioned above, in the metals ratio 70:30, was weighed in a sample boat and placed in a volatilization zone. (Total complex 0.4273g; Ni 0.0415g, Cu O.019g). The system was initially flushed with nitrogen. Then hydrogen (15 * 5 cm3/min) was introduced into the system. The substrate, mounted on a heating probe, was brought to a steady state temperature (400 * 100C) before the complex mixture was heated to its volatilization temperature of 1800C and held for a period of 1 hr.
Porosity of the resulting NiCu alloy deposit on the mild steel substrate was determined using a chemical staining technique, incorporating a sensitivity test for the substrate metal. A piece of filter paper was dipped into a solution of hexacyanoferrate (III), then pressed lightly on to the thin deposit. Although a quantitive result was not obtained from the test, it gave an indication as to the porosity of the deposit, in that any holes in the deposit resulted in a blue stain on the filter paper.
EXAMPLE 2: NiFe alloy is deposited on mild steel by depositing Ni and relying on the freshly liberated ligand to react with the substrate iron, the iron complex then being decomposed alongside the nickel complex.
In this case, the nickel complex used was nickel bis 1,1,1-trifluoro-2,4-pentanedioate, Ni(tfa)2 for short. Ni(tfa)2, 0.4344 g, was weighed in a sample boat and placed in a volatization zone. The system was initially flushed with nitrogen. Then hydrogen (10 ffi 5 cm3/min) was introduced into the system. The mild steel substrate, mounted on a heating probe, was heated to 400 * 100C before the complex was vapourised over a period of 1 hr at a temperature of 1900C.
Cross-sectional analysis of the coated substrate, using an energy dispersive X-ray analyser, showed Interpenetration of the base metal (steel) into the coating (nickel). Quantitive results have indicated the migration of iron to the nickel to be as high as 11% in cases where the coating has been 'built-up' during a number of separate runs.
EXAMPLES 3 - 5: NiCu alloy is deposited on silica glass/on alumina/on aluminium.
In each case a thin yet non-porous coherent and adherent film of alloy was achieved, at a temperature low enough not to damage the substrate, even with substrates having awkward grooves and undercuts; that is, the method has good throwing power.
In Example 5 (aluminium substrate) in particular, the operating conditions were identical to Example 1.
Initial microhardness measurements of cross-sectional pieces of coated substrate (mounted in plastics) have indicated that the deposit in some cases is harder than the substrate. However, these results are tentative where the deposit is extremely thin, such as 10 zm.
EXAMPLE 6: Coating powder particles can radically alter their properties. The coatings may only be a few atoms thick - less than 1% of the weight of the powder, yet be effective. In this example, metallic copper is deposited on supermagnetic flakes, %mm x 'kmm x 1/iomm for example, of iron neodymium boride Fel4NdB, known as Magnequench, or equally successfully on 5-micron Fel4NdB powder known as 814.
This copper provides a non-magnetic 'insulation'; on compressing the flakes (or powder particles), a small-domain highly magnetic material is obtained. This task would be difficult to achieve using conventional metal paint, and is conventionally performed by tumbling the flakes with copper powder in a process known as 'tumble-co-milling', which cannot yield the same uniformity of magnetic insulation without greater volumetric dllution of the supermagnetic material.
A copper complex consisting of the compound 2,2,6,6-tetramethyl-3,5-heptadione described above, two molecules of which complex each copper atom, was used.
B14 is very pyrophoric and is therefore stored under cyclohexane. The copper complex is dissolved directly into this, in an amount depending on the thickness of copper coating required after calculating the particle surface area; for magnetic purposes the coating thickness should be the minimum which will survive compression without rupturing. In this example, the complex was calculated to amount to 1t (based on copper) by mass of the 814. The same procedure, using cyclohexane, was also used with Magnequench. The mixture was shaken thoroughly at room temperature. The solvent cyclohexane was evaporated under nitrogen at 1000C before increasing the temperature of the system and changing to a hydrogen atmosphere to deposit the copper on the Fel4NdB at operating temperatures of 2100C for 1 hour.At much lower temperatures, the complex will not give up the copper at an adequate speed, while at much higher temperatures, the liberated dione may attack and extract the substrate Fel4NdB.
Good coverage of the Fel4NdB with copper was established by visual inspection, and by noting in the case of 814 that the product was not pyrophoric. In some cases it may be advantageous as a final step to dry tumble the coated material to assist good overall coverage.
The hydrogen gas reduces the complex, yielding elemental solid metal and liberating, in the gas phase, the initial chelating ligand. Initial n.m.r. and i.r. studies on the collected products have shown that whilst a number of ligands can be regenerated to some 'purity', especially straight chain alkane 13-diketones, their fluorinated derivatives are prone to some decomposition.
EXAMPLE 7: In other applications, the copper complex of Example 6 dissolved in cyclohexane or dimethyl ether was brush painted onto a substrate, which was heated to 2100C for 1 hour in hydrogen. A continuous copper coating was left on the substrate, and the liberated ligand could be recycled to make further paint.
EXAMPLE 8: In another application, the copper complex of Example 6 in solution was jetted, through an atomising nozzle, as a fine spray into a chamber containing hydrogen at 250"C. Copper powder was recovered from the chamber. The liberated ligand could be recycled. Care must be taken to avoid an undue proportion of the complex from decomposing on the chamber walls and simply plating them, for example a cyclonic gas flow path may be established within the chamber so that the complex does not contact the chamber wall.
A mixture of such compounds may be used, in the same or separate sprays, to yield a mixture of liberated metals, in precalculated volumetric proportions of liquid to yield the metals in the desired ratios.
Preferably the metal is one or more of a mixture of copper and nickel.
A mixture of such metal powders may permit alloys to be made by pressure-sintering which would otherwise be unobtainable or only obtainable by extraordinary techniques such as implantation by nuclear bombardment.

Claims (18)

1. A method of forming a mixed-metals coating on a surface, comprising decomposing at the surface a fluid comprising: a first compound between a first metal and a polydentate reagent, and a second compound between a second metal and the same or another polydentate reagent, wherein the reagent(s) is/are volatile, whereby the metals are co-deposited on the surface.
2. A method according to Claim 1, wherein the said second metal is the surface and wherein the said second compound is formed from reagent liberated upon decomposition of the first compound.
3. A method according to either preceding claim, wherein the decomposition is by reduction.
4. A method according to Claim 3 wherein the reduction is performed by a gas or gases.
5. A method according to any preceding claim, wherein the donor atoms of the said reagent are any selection from N, 0 and S.
6. A method according to anypreceding claim, wherein the said reagent (or one of said reagents) is a Schiff base reagent or a p-diketone.
7. A method according to any preceding claim, wherein one of the metals Is copper.
8. A method according to any preceding claim, wherein one of the metals is nickel.
9. A method according to any preceding claim, wherein said first compound is volatile.
10. A method according to any preceding claim, wherein said second compound is volatile.
11. A method according to any preceding claim, wherein said fluid is a vapour.
12. A method according to any of Claims 1-8, wherein said fluid is a liquid.
13. A method according to any preceding claim, wherein the surface is of metal, glass or ceramic or is a membrane.
14. A metallic paint, comprising a compound between the metal or each of the metals of the paint and a polydentate reagent, said compound(s) being dissolved in a paintable solvent.
15. A paint according to Claim 14, wherein the donor atoms of said reagent(s) are any selection of N, 0 and S.
16. A method of painting an object, comprising applying thereto a paint according to any preceding claim, allowing the solvent to evaporate, and applying a gaseous or volatile substance which can decompose said compound(s) to release said metal(s).
17. A method of painting according to Claim 16, wherein said compound or at least one of said compounds is dissolved in said solvent after the object has been placed in the solvent.
18. A method of making metal powder, comprising atomising a paint according to Claim 14, and applying a gaseous substance which decomposes said compound(s) to release said metal(s).
GB9002268A 1989-02-02 1990-02-01 Forming a metal coating Withdrawn GB2229453A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GB898902312A GB8902312D0 (en) 1989-02-02 1989-02-02 Making metal powder
GB898902311A GB8902311D0 (en) 1989-02-02 1989-02-02 Metallic paint
GB898902310A GB8902310D0 (en) 1989-02-02 1989-02-02 Forming mixed-metal coating

Publications (2)

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GB9002268D0 GB9002268D0 (en) 1990-03-28
GB2229453A true GB2229453A (en) 1990-09-26

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GB9002268A Withdrawn GB2229453A (en) 1989-02-02 1990-02-01 Forming a metal coating

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EP (1) EP0456679A1 (en)
JP (1) JPH04503085A (en)
CA (1) CA2046335A1 (en)
GB (1) GB2229453A (en)
WO (1) WO1990008844A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102008029691A1 (en) * 2008-06-24 2009-12-31 Leibniz-Institut Für Neue Materialien Gemeinnützige Gmbh Mixtures of precursors for the production of ceramic layers by means of MOCVD

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GB872610A (en) * 1958-03-07 1961-07-12 Union Carbide Corp Gas plating of aggregates
GB949977A (en) * 1960-06-30 1964-02-19 Sperry Rand Corp Production of magnetic films
GB964631A (en) * 1961-12-01 1964-07-22 Degussa Electrode for electrolytic processes
GB1109890A (en) * 1965-12-21 1968-04-18 Int Nickel Ltd Preparation of finely divided metals
GB1151938A (en) * 1965-09-14 1969-05-14 Asea Ab Method of Producing a Porous Electrode Material
GB1523171A (en) * 1974-08-23 1978-08-31 Schladitz Hermann J Process for the manufacture of a heat exchanger or heat transfer element
GB1527294A (en) * 1975-09-29 1978-10-04 Engelhard Min & Chem Ceramic decoration having bright white metal appearance
US4250210A (en) * 1977-12-27 1981-02-10 The International Nickel Co., Inc. Chemical vapor deposition

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US3092511A (en) * 1958-11-19 1963-06-04 Sperry Rand Corp Magnetic devices and preparation thereof
US3092510A (en) * 1959-03-02 1963-06-04 Sperry Rand Corp Magnetic devices and preparation thereof
US3071493A (en) * 1961-11-15 1963-01-01 Ethyl Corp Metal plating process
FR1406882A (en) * 1963-09-13 1965-07-23 Ass Chem Co Improvements to surface coating
NL6505307A (en) * 1964-06-25 1965-12-27
GB1249623A (en) * 1967-05-24 1971-10-13 Secr Defence Improvements in or relating to metal coatings
US3594216A (en) * 1969-06-19 1971-07-20 Westinghouse Electric Corp Vapor phase deposition of metal from a metal-organic beta-ketoamine chelate
US3615888A (en) * 1969-09-04 1971-10-26 American Cyanamid Co Chemical treatment of metal
CA935336A (en) * 1970-05-29 1973-10-16 V. Melnikov Valery Method of depositing inorganic coatings from vapour phase
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FR2314263A1 (en) * 1975-06-13 1977-01-07 Anvar Vacuum vapour deposition of metals or metalloids - by thermal decomposition of their coordination cpds. with (2,2')-bipyridyl

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB872610A (en) * 1958-03-07 1961-07-12 Union Carbide Corp Gas plating of aggregates
GB949977A (en) * 1960-06-30 1964-02-19 Sperry Rand Corp Production of magnetic films
GB964631A (en) * 1961-12-01 1964-07-22 Degussa Electrode for electrolytic processes
GB1151938A (en) * 1965-09-14 1969-05-14 Asea Ab Method of Producing a Porous Electrode Material
GB1109890A (en) * 1965-12-21 1968-04-18 Int Nickel Ltd Preparation of finely divided metals
GB1523171A (en) * 1974-08-23 1978-08-31 Schladitz Hermann J Process for the manufacture of a heat exchanger or heat transfer element
GB1527294A (en) * 1975-09-29 1978-10-04 Engelhard Min & Chem Ceramic decoration having bright white metal appearance
US4250210A (en) * 1977-12-27 1981-02-10 The International Nickel Co., Inc. Chemical vapor deposition

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102008029691A1 (en) * 2008-06-24 2009-12-31 Leibniz-Institut Für Neue Materialien Gemeinnützige Gmbh Mixtures of precursors for the production of ceramic layers by means of MOCVD

Also Published As

Publication number Publication date
EP0456679A1 (en) 1991-11-21
JPH04503085A (en) 1992-06-04
WO1990008844A1 (en) 1990-08-09
GB9002268D0 (en) 1990-03-28
CA2046335A1 (en) 1990-08-03

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