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Process for the use of metal carbonyls for the production of nano-scale metal particles formed of non-noble metals

a technology of metal carbonyl and nano-scale metal particles, which is applied in the direction of catalyst activation/preparation, cell components, physical/chemical process catalysts, etc., can solve the problems of difficult and expensive process operation, high temperature of bianchini methods, and inability to discharge carrier particles in the amount of time the loading reaction takes, so as to facilitate the flow of reactants and relieve pressure build-up

Inactive Publication Date: 2007-02-15
DIRECTA PLUS
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

[0022] The reactor vessel can be formed of any material which can withstand the conditions under which the decomposition of the carbonyl occurs. Generally, where the reactor vessel is a closed system, that is, where it is not an open ended vessel permitting reactants to flow into and out of the vessel, the vessel can be under subatmospheric pressure, by which is meant pressures as low as about 250 millimeters (mm). Indeed, the use of subatmospheric pressures, as low as about 1 mm of pressure, can accelerate decomposition of the carbonyl and provide smaller nano-scale particles. However, one advantage of the inventive process is the ability to produce nano-scale particles at generally atmospheric pressure, i.e., about 760 mm. Alternatively, there may be advantage in cycling the pressure, such as from sub-atmospheric to generally atmospheric or above, to encourage nano-deposits within the structure of the carrier particles or supports. Of course, even in a so-called “closed system,” there needs to be a valve or like system for relieving pressure build-up caused, for instance, by the generation of carbon monoxide (CO) from decomposition of the metal carbonyl or other by-products. Accordingly, the use of the expression “closed system” is meant to distinguish the system from a flow-through type of system as discussed hereinbelow.
[0040] It is another object of the present invention to provide a process capable of producing non-noble metal nano-scale particles under conditions of temperature and / or pressure less extreme than conventional processes.

Problems solved by technology

One major drawback to the preparation of catalyst materials through loading on a carrier particle is in the amount of time the loading reactions take, which can be measured in hours in some cases.
Thus, these processes are difficult and expensive to operate and also involve line-of-sight reactions, precluding fully utilization of the support structure.
Even if technically feasible, however, the Bert and Bianchini methods require high temperatures (on the order of 300° C. to 800° C.)
, and require several hours. A
ccordingly, these processes are of limited value.
However, more significant uses of metal carbonyls are in the production and / or deposition of the metals present in the carbonyl, since metal carbonyls are generally viewed as easily decomposed and volatile resulting in deposition of the metal and carbon monoxide.

Method used

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  • Process for the use of metal carbonyls for the production of nano-scale metal particles formed of non-noble metals
  • Process for the use of metal carbonyls for the production of nano-scale metal particles formed of non-noble metals
  • Process for the use of metal carbonyls for the production of nano-scale metal particles formed of non-noble metals

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[0052] Referring now to the drawings, an apparatus for the production of non-noble metal nano-scale particles is generally designated by the numeral 10 or 100. In FIGS. 1 and 2 apparatus 10 is a closed system comprising closed reactor vessel 20 whereas in FIGS. 3-5 apparatus 100 is a flow-through reaction apparatus comprising flow-through reactor vessel 120.

[0053] It will be noted that FIGS. 1-5 show apparatus 10, 100 in a certain orientation. However, it will be recognized that other orientations are equally applicable for apparatus 10. For instance, when under vacuum, reactor vessel 20 can be in any orientation for effectiveness. Likewise, in flow-through reactor vessel 120, the flow of inert carrier gas and metal carbonyls or the flow of metal carbonyls as drawn by a vacuum (or combinations thereof in FIGS. 3-5 can be in any particular direction or orientation and still be effective. In addition, the terms “up”“down”“right” and “left” as used herein refer to the orientation of a...

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Abstract

A process for producing nano-scale metal particles includes feeding at least one metal carbonyl into a reactor vessel; exposing the metal carbonyl to a source of energy sufficient to decompose the metal carbonyl and produce nano-scale metal particles; and depositing or collecting the nano-scale metal particles.

Description

TECHNICAL FIELD [0001] The present invention relates to a process for the production of non-noble metal nano-scale particles using metal carbonyls. By “non-noble metal” is meant a metal other than one of the noble metals (generally considered to be gold, silver, platinum, palladium, iridium, rhenium, mercury, ruthenium and osmium). The resulting nano-scale particles are useful for catalysis and other purposes. By the practice of the present invention, nano-scale particles can be produced from metal carbonyls and collected with greater speed, precision and flexibility than can be accomplished with conventional processing. Thus, the invention provides a practical and cost-effective means for preparing such nano-scale particles. BACKGROUND OF THE INVENTION [0002] Catalysts are becoming ubiquitous in modern chemical processing. Catalysts are used in the production of materials such as fuels, lubricants, refrigerants, polymers, drugs, etc., as well as playing a role in water and air poll...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): B22F9/28
CPCB01J35/0013B01J37/086B22F9/305B22F2998/00H01M4/90B22F2201/10B22F2201/20B22F2202/11Y02E60/50B01J35/23
Inventor MERCURI, ROBERT A.
Owner DIRECTA PLUS
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