WO1981002688A1 - A liquid suspension of particles of a metal belonging to the platinum group,and a method for the manufacture of such a suspension - Google Patents

A liquid suspension of particles of a metal belonging to the platinum group,and a method for the manufacture of such a suspension Download PDF

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Publication number
WO1981002688A1
WO1981002688A1 PCT/SE1981/000091 SE8100091W WO8102688A1 WO 1981002688 A1 WO1981002688 A1 WO 1981002688A1 SE 8100091 W SE8100091 W SE 8100091W WO 8102688 A1 WO8102688 A1 WO 8102688A1
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WIPO (PCT)
Prior art keywords
suspension
particles
microemulsion
metal
platinum group
Prior art date
Application number
PCT/SE1981/000091
Other languages
French (fr)
Inventor
P Stenius
M Boutonnet
J Kizling
Original Assignee
Ytkemiska Inst
P Stenius
M Boutonnet
J Kizling
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Filing date
Publication date
Application filed by Ytkemiska Inst, P Stenius, M Boutonnet, J Kizling filed Critical Ytkemiska Inst
Priority to DE8181900804T priority Critical patent/DE3161354D1/en
Publication of WO1981002688A1 publication Critical patent/WO1981002688A1/en
Priority to DK514181A priority patent/DK158709C/en
Priority to FI821138A priority patent/FI66765C/en

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/20—Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state
    • B01J35/23—Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state in a colloidal state
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/56—Platinum group metals
    • B01J23/62—Platinum group metals with gallium, indium, thallium, germanium, tin or lead
    • B01J23/622—Platinum group metals with gallium, indium, thallium, germanium, tin or lead with germanium, tin or lead
    • B01J23/628—Platinum group metals with gallium, indium, thallium, germanium, tin or lead with germanium, tin or lead with lead
    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B11/00—Obtaining noble metals

Definitions

  • the invention relates to a liquid suspension of particles of a metal belonging to the platinum group, and a method for the manufacture of such a suspension.
  • the suspension of the invention is useful, for example, for manufacturing catalysts by depositing the metal particles on a carrier.
  • the platinum group comprises ruthenium, rhodium, palladium, osmium, iridium, and platinum.
  • the invention aims at ele inating said incon ⁇ veniences.
  • the suspension of the invention is characte-r-- ized in that the liquid in which the metal particles are suspended consists of a microemulsion.
  • the invention also relates to a method for manufacturing the suspension.
  • the method is characterized by reducing a metal salt dissolved in a microemulsion.
  • Microemulsions have been known for about three decades. They consist of transparent, thermodynamically stable solutions of water and hydrocarbons, stabilized by a surfactant and, if desired, a second substance having a carbon chain of medium length and a polar end group, for example an aliphatic alcohol or a fatty acid.
  • the surfactant should be a non-ionic compound soluble in the hydro ⁇ carbon.
  • the non-ionic compound shall not react with the reducing agent, meaning that it shall not contain double bonds or other characteristic groups which can be reduced (hydrated) .
  • the non-ionic compound shall not, for example, have aromatic groups in the hydrocar ⁇ bon chain. This demand is met by non-ionic surfactants . having been synthetized by .
  • the non-ionic compounds shall be insoluble in the solvents present in the microemulsion.
  • These demands eliminate several classes of non-ionic surfactants, for example those having been formed by an esterification process, because they are reduced by, or form a precipitation with, hydrazine.
  • polyethyleneglycol alkylethers preferably containing 12-14 carbon atoms in the carbon chain, and 2-8 ethyleneoxide units in the polyethyleneglycol chain, for example tetraethyleneglycol dodecylether.
  • the hydrocarbon shall not react chemically with the other components of the solution, or with the reducing agents, which are very reactive. This demand eliminates, for example, aromatic hydrocarbons which react with the re- ducing agents.
  • the metal salt shall be soluble in the icro- emulsion.
  • the salt can be dissolved in a small quantity of water, and the aqueous solution thus produced may be mixed into a mixture of the surfactant and the hydrocarbon.
  • the meatl salt which usually contains some crystal water, may be dissolved in the surfactant, and the solution may be mixed with the hydrocarbon, and accitional water may finally be added, if desired.
  • the metal compound may be any simple salt, or the corresponding acid, which is soluble in alcohols and/or water. W r hen preparing a platinum suspension we prefer to use chloroplatinic acid, H 2 PtCl fi " H_0, in which x is 6 at most.
  • platinum compounds are sodiumhexachloroplatinate, Na 2 PtClg-6H 2 0, sodiumhexabromoplatinate, Na 2 PtBr 6 «6H 2 0, and hexabromoplatinic acid, H-PtBr fi • ⁇ H ⁇ O.
  • Useful salts for the manufacture of suspensions of the other platinum group metals are, for example, palladium chloride, PdCl 7 , sodiumhexachloropalladinate, Na 2 PdClg, sodiumtetra- chloropalladinate, Na 2 PdCl, • 3H 2 0, ruthenium chloride, RuCl ⁇ 'X H 2 0, iridium chloride, IrCl ⁇ -x H 2 0, hexachloro- iridic acid, H 2 IrCl 6 -x H 2 0, osmium tetraoxide, OsO ⁇ , rhodium chloride, RhCl.,'H ? 0.
  • Fig. 1 shows a portion of a ternary diagram representing a microemulsion useful for making a suspension according to the invention.
  • Fig. 2 shows a ternary diagram representing the micro ⁇ emulsion formed upon adding chloroplatinic acid and crystal water to the microemulsion represented by Fig. 1.
  • Fig. 3 shows part of the ternary diagram of Fig. 2 on a larger scale.
  • the upper corner of the triangle represents 100 per cent by weight n-hexane
  • the lower right-hand corner represents 20 per cent by weight pentaethyleneglycol dodecylether (PEGDE)
  • PEGDE pentaethyleneglycol dodecylether
  • the lower left-hand corner represents 20 per cent by weight water.
  • the area L ⁇ represents a microemulsion, i.e. an isotropic, clear solution.
  • the diagram is true for a temperature of 23 C.
  • the area L ⁇ will have other shapes at other temperatures.
  • a high percentage of surfactant makes the suspension difficult to handle, for example when using the metal particles as a catalyst. Therefore, we prefer to use only the upper, shaded portion of the area L 2 , viz. the area in which the percentage of hydrocarbon in the microemulsion is above approximately 80 per cent by weight and the percentage of PEGDE is below approximately 20 per cent by weight. If an aqueous solution of chloroplatinic acid is added to the microemulsion of Fig.
  • the result will be a micro ⁇ emulsion represented by the diagram of Fig. 2.
  • the upper corner of the triangle represents 100 per cent by weight n-hexane
  • the right- -hand bottom corner represents 100 per cent by weight pentaethyleneglycol dodecylether (PEGDE)
  • PEGDE pentaethyleneglycol dodecylether
  • ⁇ ⁇ UE -hand bottom corner represents 100 per cent by weight chloroplatinic acid plus crystal water.
  • the diagram is true for a temperature of 23°C.
  • the preferred portion of the area L 2 is shaded, and is disclosed on a larger scale by Fig. 3.
  • a practical application of the diagram of Fig. 3 is illustrated by Example 1.
  • the diagram of Figs. 2 and 3 discloses that the smallest required percentage of PEGDE is approximately 5 per cent by weight, and the smallest percentage of water + chloroplatinic acid that can be dissolved in the micro ⁇ emulsion is approximately 5 per cent by weight.
  • the finished suspension will have a maximum of stability if the weight ratio PEGDE to chloroplatinic acid is higher than 20.
  • the metal salt is chloroplatinic acid
  • hydrogen chloride will be formed as a by-product. Consequently, the pH of the microemulsion will sink. Too low a pH will reduce the stability of the finished suspension. Therefore, we prefer to increase, before the reduction, the pH of the microemulsion to 9-10 by adding an aqueous solution of sodium hydroxide. This will result in a pH of 4-6- after the reduction, and the stability is not impaired.
  • the reduction can be brought about in a simple way by adding the microemulsion, containing a dissolved metal salt, to a glass flask, adding the reducing agent in liquid or gaseous form to said flask, and shaking the flask for a few minutes at room tempera ⁇ ture.
  • each "droplet" of water in the microemulsion acts as a crystallization nucleus during the reduction.
  • Each "droplet” contains a plurality of molecules of the metal salt. The number of crystallization nuclei will be comparatively high, and the nuclei are separated from each other by a medium in which ' the reduced compound is insoluble.
  • the finished metal particles are likely to have approximately the same size, which is consistent with our experience.
  • the particle size lies within a narrow range. Usually a particle diameter is obtained having a standard deviation from the average diameter of less than - 10 % .
  • the suspension of the invention can be used for making a catalyst, either with the metal particles still being suspended in the solution, or by depositing the metal particles on a solid carrier, for example pumice or pulverulent A1 2 0,.
  • a solid carrier for example pumice or pulverulent A1 2 0,.
  • the following depositing process is preferred, to prevent the metal particles from agglomerating to form bigger aggregates.
  • the solid carrier is moistened with the suspension, and the liquid of the microemulsion is evaporated, preferably by exposing the moistened carrier to a reduced pressure. This process is repeated until the carrier possesses • the desired density of the metal particles.
  • the sur ⁇ factant is now removed by rinsing the carrier repeatedly with ethanol.
  • the carrier is finally dried at a reduced pressure.
  • Berol 050 a polyethyleneglycol alkylehter
  • H 2 PtCl 6 » H 2 0 was added in a quantity equivalent with approximately 4 x 10 " grams metallic platinum per gram of solution. This means that the solution will contain approximately 0.3 grams water.
  • Sodium hydroxide was added as a solution containing 1 mol per dm , in a quantity equivalent with the hydrochloric acid to be formed during the reduction. The platinum salt was now
  • hydroxide having a concentration of 1 mol per dm was added in a quantity adequate for neutralizing the hydro ⁇ chloric acid expected to be formed during the reduction.
  • the palladium salt was now reduced by the addition of hydrazine.
  • the hydrazine was added in an excess, so as to compensate for the hydrazine being decomposed by the formed solid palladium.
  • the reduction runs fast at room temperature, and creates palladium particles having a diameter of approximately 5.0 nm.
  • the final pH of the suspension was 5-6.
  • the rhodium salt was now reduced by hydrogen which was made to pass through the solution. The reduction was completed after approximately 2.5 hours at a temperature of 23 C.
  • the rhodium particles of the finished suspension had a diameter of approximately 3.0 nm.
  • the suspension had a pH of 5-6.
  • a mixture was prepared consisting of 8.8 grams cyclohexane and 1.0 gram Berol 050. The Berol had been purified by vacuum distillation. To this mixture was added H-PtClg-x H 2 0 dissolved in 2.0 grams water. The quantity of the platinum salt was chosen to correspond to 2.2 x 10 -4 gram metallic platinum per gram solution. Sodium hydroxide was added in a quantity adequate to neutralize the hydrochloric acid to be formed. The sodium hydroxide added as a solution containing 1 ol per dm .
  • the platinum salt was now reduced by the addition of an excess of hydrazine while stirring. It was neces ⁇ sary to add the hydrazine in an excess because it is. decomposed by the formed solid platinum.
  • the reaction runs fast at room temperature, and results in a stable suspension of platinum particles having a size of approximately 2.5 - 0.2 nm.
  • the pH of the suspension is 5-6, and the correct quantity of added hydraz be controlled by said pH being attained.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
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Abstract

A stable suspension of particles of a metal belonging to the platinum group consists of a microemulsion in which the particles are suspended. The suspension is prepared by dissolving a metal salt in a microemulsion, and reducing the salt to form a metal.

Description

A LIQUID SUSPENSION OF PARTICLES OF A METAL BELONGING TO THE PLATINUM GROUP, AND A METHOD FOR THE MANUFACTURE OF SUCH A SUSPENSION
TECHNICAL FIELD The invention relates to a liquid suspension of particles of a metal belonging to the platinum group, and a method for the manufacture of such a suspension. The suspension of the invention is useful, for example, for manufacturing catalysts by depositing the metal particles on a carrier. The platinum group comprises ruthenium, rhodium, palladium, osmium, iridium, and platinum.
BACKGROUND ART It is well known to prepare a suspension of platinum particles by reducing a platinum salt in an aqueous solution with hydrogen, for example. The platinum particles thus produced usually have an average size of at least 10 nm. The suspension, however, contains particles of various sizes, which is due to the fact that small particles have a tendency to unite to form bigger particles during the reduction. This is a disadvantage if the particles are to be used for catalytic purposes, because in this case small particles of approximately the same size are desired. It is another inconvenience that the suspension referred to is not quite stable.The particles have a tendency to settle.
DISCLOSURE OF INVENTION The invention aims at ele inating said incon¬ veniences. The suspension of the invention is characte-r-- ized in that the liquid in which the metal particles are suspended consists of a microemulsion. The invention also relates to a method for manufacturing the suspension.
-^ΌREA^ "-' The method is characterized by reducing a metal salt dissolved in a microemulsion.
Microemulsions have been known for about three decades. They consist of transparent, thermodynamically stable solutions of water and hydrocarbons, stabilized by a surfactant and, if desired, a second substance having a carbon chain of medium length and a polar end group, for example an aliphatic alcohol or a fatty acid. When used in the present invention the surfactant should be a non-ionic compound soluble in the hydro¬ carbon. The non-ionic compound shall not react with the reducing agent, meaning that it shall not contain double bonds or other characteristic groups which can be reduced (hydrated) . The non-ionic compound shall not, for example, have aromatic groups in the hydrocar¬ bon chain. This demand is met by non-ionic surfactants . having been synthetized by. reacting ethyleneoxide oligomers with higher aliphatic alcohols so that they are bonded to the hydrocarbon chain with an ether bond, for example pentaethyleneglycol dodecylether-and its homologes. The non-ionic compounds shall be insoluble in the solvents present in the microemulsion. These demands eliminate several classes of non-ionic surfactants, for example those having been formed by an esterification process, because they are reduced by, or form a precipitation with, hydrazine. We prefer to use polyethyleneglycol alkylethers, preferably containing 12-14 carbon atoms in the carbon chain, and 2-8 ethyleneoxide units in the polyethyleneglycol chain, for example tetraethyleneglycol dodecylether. The hydrocarbon shall not react chemically with the other components of the solution, or with the reducing agents, which are very reactive. This demand eliminates, for example, aromatic hydrocarbons which react with the re- ducing agents. The boiling temperature of the hydro-
- TJR
S2. carbon shall not be close to the temperature at which the metal particles are precipitated, because this would result in a heavy evaporation of the hydro¬ carbon when gaseous reaction products leave the microemulsion.' The following types of hydrocarbons are useful, fiz: Aliphatic non-cyclic hydrocarbons, for example the homologous series hexane - hexadecane, including branched isomers; aliphatic cyclic hydrocarbons, for example cyclohexane, methyl-cyclohexane, dimethyl- cyclohexanes and other cyclohexane derivatives, decahydro- naphtalene. If the particles are to be deposited on a carrier it is preferred to use readily volatile alkanes (6-10 carbon atoms).
The metal salt shall be soluble in the icro- emulsion. The salt can be dissolved in a small quantity of water, and the aqueous solution thus produced may be mixed into a mixture of the surfactant and the hydrocarbon. Alternatively, the meatl salt, which usually contains some crystal water, may be dissolved in the surfactant, and the solution may be mixed with the hydrocarbon, and accitional water may finally be added, if desired. The metal compound may be any simple salt, or the corresponding acid, which is soluble in alcohols and/or water. Wrhen preparing a platinum suspension we prefer to use chloroplatinic acid, H2PtClfi" H_0, in which x is 6 at most. Other useful platinum compounds are sodiumhexachloroplatinate, Na2PtClg-6H20, sodiumhexabromoplatinate, Na2PtBr6«6H20, and hexabromoplatinic acid, H-PtBrfi •όH^O. Useful salts for the manufacture of suspensions of the other platinum group metals are, for example, palladium chloride, PdCl7, sodiumhexachloropalladinate, Na2PdClg, sodiumtetra- chloropalladinate, Na2PdCl, • 3H20, ruthenium chloride, RuCl^'X H20, iridium chloride, IrCl^-x H20, hexachloro- iridic acid, H2IrCl6-x H20, osmium tetraoxide, OsO^, rhodium chloride, RhCl.,'H?0.
-^U EA o~.~?ι DESCRIPTION OF THE INVENTION WITH REFERENCE TO THE DRAWINGS
The invention will now be described with reference to the drawings. Fig. 1 shows a portion of a ternary diagram representing a microemulsion useful for making a suspension according to the invention. Fig. 2 shows a ternary diagram representing the micro¬ emulsion formed upon adding chloroplatinic acid and crystal water to the microemulsion represented by Fig. 1. Fig. 3 shows part of the ternary diagram of Fig. 2 on a larger scale. In the ternary diagram disclosed on Fig. 1 the upper corner of the triangle represents 100 per cent by weight n-hexane, the lower right-hand corner represents 20 per cent by weight pentaethyleneglycol dodecylether (PEGDE) , and the lower left-hand corner represents 20 per cent by weight water. The area L~ represents a microemulsion, i.e. an isotropic, clear solution. The diagram is true for a temperature of 23 C. The area L~ will have other shapes at other temperatures. A high percentage of surfactant makes the suspension difficult to handle, for example when using the metal particles as a catalyst. Therefore, we prefer to use only the upper, shaded portion of the area L2, viz. the area in which the percentage of hydrocarbon in the microemulsion is above approximately 80 per cent by weight and the percentage of PEGDE is below approximately 20 per cent by weight. If an aqueous solution of chloroplatinic acid is added to the microemulsion of Fig. 1, for making a suspension according to the invention, the result will be a micro¬ emulsion represented by the diagram of Fig. 2. In the diagram of Fig. 2 the upper corner of the triangle represents 100 per cent by weight n-hexane, the right- -hand bottom corner represents 100 per cent by weight pentaethyleneglycol dodecylether (PEGDE), and the left-
■^UE -hand bottom corner represents 100 per cent by weight chloroplatinic acid plus crystal water. The diagram is true for a temperature of 23°C. The preferred portion of the area L2 is shaded, and is disclosed on a larger scale by Fig. 3. A practical application of the diagram of Fig. 3 is illustrated by Example 1. The diagram of Figs. 2 and 3 discloses that the smallest required percentage of PEGDE is approximately 5 per cent by weight, and the smallest percentage of water + chloroplatinic acid that can be dissolved in the micro¬ emulsion is approximately 5 per cent by weight. The finished suspension will have a maximum of stability if the weight ratio PEGDE to chloroplatinic acid is higher than 20. Ternary diagrams of the type illustrated on the drawing can be produced for each combination of hydrocarbon, surfactant,- water, and metal salt. How to determine the boundary of the area L2 has been dis¬ closed by S. Friberg and. I . Lapczynska: Progr. Colloid & Polymer Sci. _56_, 16-20 (1975). Said article also gives some literature references on microemulsions . The reducing agent should not produce any by- -products which destroy the microemulsion or change the area in which it can exist. Therefore, substances pro¬ ducing insoluble solid or liquid reaction products, in addition to metal particles, are not suitable as re¬ ducing agents. We prefer to use hydrogen and h drazine, NH2'NH2. Other useful reducing agents are aldehydes, for example formaldehyde HCHO.
If the metal salt is chloroplatinic acid, hydrogen chloride will be formed as a by-product. Consequently, the pH of the microemulsion will sink. Too low a pH will reduce the stability of the finished suspension. Therefore, we prefer to increase, before the reduction, the pH of the microemulsion to 9-10 by adding an aqueous solution of sodium hydroxide. This will result in a pH of 4-6- after the reduction, and the stability is not impaired. The reduction can be brought about in a simple way by adding the microemulsion, containing a dissolved metal salt, to a glass flask, adding the reducing agent in liquid or gaseous form to said flask, and shaking the flask for a few minutes at room tempera¬ ture. By shaking vigorously the reduction time may be brought down to approximately 1/2 minute, which is favourable for the stability of the finished suspension. .'.Jithout committing ourselves to any theory on the formation and growth of the metal crystals during the reduction, we believe that each "droplet" of water in the microemulsion acts as a crystallization nucleus during the reduction. Each "droplet" contains a plurality of molecules of the metal salt. The number of crystallization nuclei will be comparatively high, and the nuclei are separated from each other by a medium in which' the reduced compound is insoluble. This is likely to mean that the formation of crystals can start simultaneously in each crystallization nucleus, and that the crystal growth can continue on each crystal as long as the microemulsion contains any unreduced metal salt. Conseuently, the finished metal particles are likely to have approximately the same size, which is consistent with our experience. In fact, it is a characteristic feature of the suspension of the invention that the particle size lies within a narrow range. Usually a particle diameter is obtained having a standard deviation from the average diameter of less than - 10 % . For example, when manufacturing a suspension of platinum particles in which 70 % of the total number of particles had a size very close to 2.5 nm wre found that only 12 % o the particles had a size between 2.2 and 2.4 n , and that only 18 % of the particles had a size between 2.5 and 2.7 nm. The particle diameter was determined by means of electron microscopy. The particles were transferred to the diffraction grating by applying a thin layer of the suspension on the diffraction grating, and drying said thin layer. Smaller or bigger particles had not been formed at all. The electron microscopy dis¬ closed that the particles are crystalline.
The suspension of the invention can be used for making a catalyst, either with the metal particles still being suspended in the solution, or by depositing the metal particles on a solid carrier, for example pumice or pulverulent A120,. The following depositing process is preferred, to prevent the metal particles from agglomerating to form bigger aggregates. The solid carrier is moistened with the suspension, and the liquid of the microemulsion is evaporated, preferably by exposing the moistened carrier to a reduced pressure. This process is repeated until the carrier possesses • the desired density of the metal particles. The sur¬ factant is now removed by rinsing the carrier repeatedly with ethanol. The carrier is finally dried at a reduced pressure.
EXAMPLE 1
This is an example of the manufacture of a suspen- sion of platinum particles. The commercial surfactant
Berol 050, a polyethyleneglycol alkylehter, was freed of impurities by being distilled in vacuum. 0.52 grams of the purified surfactant was dissolved in 9.45 grams n-hexane. H2PtCl6» H20 was added in a quantity equivalent with approximately 4 x 10" grams metallic platinum per gram of solution. This means that the solution will contain approximately 0.3 grams water. Sodium hydroxide was added as a solution containing 1 mol per dm , in a quantity equivalent with the hydrochloric acid to be formed during the reduction. The platinum salt was now
- fREΛl^ reduced by the addition of hydrazine in excess while stirring. It is necessary to add the hydrazine in excess, because the compound is decomposed by solid platinum. The reduction goes fast at room temperature, and produces a stable suspension of platinum particles having a diameter of approximately 2.5 - 0.2 nm. The pH of the finished suspension is 5-6. The quantity of added hydrazine can be controlled by means of the fact that said final pH shall be attained.
EXAMPLE 2
This is an example of the manufacture of a suspension of palladium particles. 0.96 gram Berol 05 was purified by distillation in vacuum, and was dissolved in 8.6 grams n-hexane. 0.31 gram aqueous solution was added, containing 5 per cent by weight
PdCl2. The palladium solution had been given a pH of
2-3 by the addition of 1 M hydrochloric acid. The quantity of palladium salt referred to corresponds to 9.4 x 10 gram palladium per gram solution. Sodium
3 hydroxide having a concentration of 1 mol per dm was added in a quantity adequate for neutralizing the hydro¬ chloric acid expected to be formed during the reduction. The palladium salt was now reduced by the addition of hydrazine. The hydrazine was added in an excess, so as to compensate for the hydrazine being decomposed by the formed solid palladium. The reduction runs fast at room temperature, and creates palladium particles having a diameter of approximately 5.0 nm. The final pH of the suspension was 5-6.
EXAMPLE 3
This is an example of the manufacture of a suspension of rhodium particles. 1.95 grams Berol 05 was purified by distillation in vacuum, and was mixed with 7.9 grams n-hexadecane. RhCl^-x H20 was added in a quantity to produce a solution containing approximate- ly 1.15 x 10 gram Rh per gram solution. Sodium carbonate in a quantity equivalent to the hydro- chloric acid expected to be formed during the reduction was dissolved in 0.15 gram water, and the solution was added to the mixture.
The rhodium salt was now reduced by hydrogen which was made to pass through the solution. The reduction was completed after approximately 2.5 hours at a temperature of 23 C. The rhodium particles of the finished suspension had a diameter of approximately 3.0 nm. The suspension had a pH of 5-6.
EXAMPLE 4
This is an example of the manufacture of a suspension of platinum particles, in which the micro¬ emulsion is based upon a cyclic aliphatic hydrocarbon. A mixture was prepared consisting of 8.8 grams cyclohexane and 1.0 gram Berol 050. The Berol had been purified by vacuum distillation. To this mixture was added H-PtClg-x H20 dissolved in 2.0 grams water. The quantity of the platinum salt was chosen to correspond to 2.2 x 10 -4 gram metallic platinum per gram solution. Sodium hydroxide was added in a quantity adequate to neutralize the hydrochloric acid to be formed. The sodium hydroxide
Figure imgf000011_0001
added as a solution containing 1 ol per dm .
The platinum salt was now reduced by the addition of an excess of hydrazine while stirring. It was neces¬ sary to add the hydrazine in an excess because it is. decomposed by the formed solid platinum. The reaction runs fast at room temperature, and results in a stable suspension of platinum particles having a size of approximately 2.5 - 0.2 nm. The pH of the suspension is 5-6, and the correct quantity of added hydraz be controlled by said pH being attained.

Claims

1. ' A licμiid suspension ofparticles of- a metal belonging to the platinum group, characterized in that the liquid consists of a microemulsion.
2. A suspension as claimed in claim 1, charac¬ terized in that the mkcroemulsion consists of a hydro¬ carbon, a non-ionic surfactant, and water.
3. A suspension as claimed in claim 1, characterized in that the metal particles have a size of 2-5 nm.
4. A suspension as claimed in claim 1, characterized in that the metal particles consist of mono-crystals.
5. A suspension as claimed in claim 1, characterized in that the size of the metal particles does not deviate from the average size by more than 10 % .
6. A suspension as claimed in claim 1, in which the microemulsion consists of n-hexane, penta¬ ethyleneglycol dodecylether, and water, characterized in that the composition of the microemulsion is re¬ presented by the shaded area in the ternary diagram disclosed in the drawing.
7. A method for the manufacture of a liquid suspension of particles of a metal belonging to the platinum group, by reducing a metal salt in an aqueous solution, characterized in dissolving the metal salt in a microemulsion, and reducing the dis¬ solved metal salt to the metallic state.
8. A method as claimed in claim 7, characterized in dissolving the metal salt in a micro¬ emulsion consisting of a hydrocarbon, a non-ionic surfactant, and water.
9. A method as claimed in claim 7, characterized in reducing the metal salt with hydrogen or hydrazine.
- uR£
_. OM?I
10. A method as claimed in claim 7, in which acid by-products are formed in the reaction, characterized in giving the microemulsion, before the reduction, such an increased pH that the pH after the reduction is at least 4.
11. The use of a suspension of particles of a metal belonging to the platinum group in a liquid consisting of a microemulsion, as a catalyst directly, or for the manufacture of a catalyst by transferring the particles to a carrier.
PCT/SE1981/000091 1980-03-24 1981-03-20 A liquid suspension of particles of a metal belonging to the platinum group,and a method for the manufacture of such a suspension WO1981002688A1 (en)

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DE8181900804T DE3161354D1 (en) 1980-03-24 1981-03-20 A liquid suspension of particles of a metal belonging to the platinum group, and a method for the manufacture of such a suspension
DK514181A DK158709C (en) 1980-03-24 1981-11-19 LIQUID SUSPENSION OF PARTICLES OF A METAL FROM THE PLATING GROUP, PROCEDURE FOR ITS PREPARATION AND ITS USE
FI821138A FI66765C (en) 1980-03-24 1982-04-01 VAETSKESUSPENSION AV PARTIKLAR AV EN METALL TILLHOERANDE PLATINAGRUPPEN OCH FOERFARANDE FOER FRAMSTAELLNING AV EN SAODAN SUSPENSION

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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1985003240A1 (en) * 1984-01-30 1985-08-01 Eka Ab Catalytic exhaust emission control device and method of making it
WO1985003241A1 (en) * 1984-01-30 1985-08-01 Eka Ab Filler or a support for catalytically active substances, a process for producing said filler or support, a catalyst produced from said support, and the use of said catalyst
WO1985003239A1 (en) * 1984-01-30 1985-08-01 Eka Ab Fine particles with a surface coating of metal or metal compound, particulalrly a catalytically active substance, and a method of producing them
EP0153911A1 (en) * 1984-01-30 1985-09-04 Eka Nobel Aktiebolag Catalytic exhaust emission control device and a method of making it
EP0580559A1 (en) * 1992-07-06 1994-01-26 Tanaka Kikinzoku Kogyo Kabushiki Kaisha Process of preparing catalyst supporting highly dispersed platinum particles
EP0804952A1 (en) * 1996-04-29 1997-11-05 Bayer Ag Process for the preparation of finely devided crystallisation products
US6074441A (en) * 1996-04-29 2000-06-13 Bayer Aktiengesellschaft Process for producing ultrafine-crystallization products
EP1985361A1 (en) * 2007-04-24 2008-10-29 Järäs, Sven Method for depositing metal particles on a support
NL2005365C2 (en) * 2010-09-17 2012-03-20 Univ Delft Tech Carbon nanostructures and networks produced by chemical vapor deposition.
WO2012036555A1 (en) 2010-09-17 2012-03-22 Delft Enterprises B.V. Carbon nanostructures and networks produced by chemical vapor deposition

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DK514181A (en) 1981-11-19
FI66765C (en) 1984-12-10
JPS57500324A (en) 1982-02-25
DE3161354D1 (en) 1983-12-15
FI821138A0 (en) 1982-04-01
FI66765B (en) 1984-08-31
NO152360B (en) 1985-06-10
DK158709C (en) 1990-12-03
NO813957L (en) 1981-11-20
US4425261A (en) 1984-01-10
JPH0251666B2 (en) 1990-11-08
DK158709B (en) 1990-07-09
EP0055257A1 (en) 1982-07-07
NO152360C (en) 1985-09-18
FI821138L (en) 1982-04-01
EP0055257B1 (en) 1983-11-09

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