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Publication numberUS3711274 A
Publication typeGrant
Publication dateJan 16, 1973
Filing dateMay 14, 1970
Priority dateMay 19, 1969
Also published asDE2024048A1, DE2024048B2, DE2024048C3
Publication numberUS 3711274 A, US 3711274A, US-A-3711274, US3711274 A, US3711274A
InventorsF Montino, F Guerrieri
Original AssigneeMontedison Spa
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Process for preparing finely particled nickel powder
US 3711274 A
Abstract
A process is disclosed for preparing finely particled metallic nickel powder, with spheroidal form, having dimensions lower than 1 micron. Bis-acrylonitrile-nickel is suspended in methanol, and the suspension is heated at temperatures between 100 DEG and 200 DEG C, and preferably at 150 DEG -180 DEG C, up to the complete decomposition. During the heating of the suspension, hydrogen is introduced under pressure.
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Description  (OCR text may contain errors)

United States Patent 1191 Montino et al.

1 51 Jan. 16, 1973 [54] PROCESS FOR PREPARING FINELY PARTICLED NICKEL POWDER [7'5] Irivehtorffihricb "Montino, C'lEMohfrrato; Franco Guerrieri, Novara,

both of Italy [22] Filed: May 14, 1970 211 App]. No.: 37,294

[30] Foreign Application Priority Data 3,573,292 3/1971 Wilke et al. ..260/242 OTHER PUBLICATIONS G. N. Schrauzer, J. Am. Chem. Soc., 81(1959), 5310-5312 Primary Examiner0scar R. Vertiz Assistant ExaminerHoke S. Miller Attorney-Stevens, Davis, Miller & Mosher [5 7] ABSTRACT A process is disclosed for preparing finely particled metallic nickel powder, with spheroidal form, having dimensions lower than 1 micron. Bis-acrylonitrilenickel is suspended in methanol, and the suspension is heated at temperatures between 100 and 200C, and preferably at l50l80C, up to the complete decomposition. During the heating of the suspension, hydrogen is introduced under pressure.

2 Claims, No Drawings PROCESS FOR PREPARING FINELY PARTICLED NICKEL POWDER The present invention relates to a process for preparing powder of metallic nickel. More particularly, it relates to a process for preparing finely divided metallic nickel powder below 1 micron in particle size, and having a spheroidal form.

Metallic powders having a spherical form with a diameter lower than 1 micron, and with a homogeneous distribution of the diameters, are used more and more in powder metallurgy because of the greater uniformity and the better properties of the end product. They are used, for example, either for making sintered alloys based on Ni-Cr-Co or based on Ni-Cr- A1 resistant to high temperatures, or for making magnetic sintered alloys based on Fe-Ni, or for making porous barriers based on nickel employed in the separation in the gaseous phase of uranium isotopes.

It is already known to produce powdered metallic nickel by thermal decomposition of nickel tetracarbonyl, of nickel oxalate and of formate. It is also known to produce powdered pure metallic nickel by the reduction of nickel oxide, nickel hydrate and nickel carbonate. The process more frequently used on an industrial scale consists in carrying out the steam pyrolysis of nickel tetracarbonyl, diluted in an inert gas, at a temperature ranging from 200 to 250C. In some cases, the decomposition is carried out in fuel oils or in biphenyl mixed with biphenyl-oxide.

Those processes involve the drawback of producing powdered nickel in which the particles have a diameter ranging from 2 to 5 microns. Such a particle size renders the metallic nickel thus obtained not very suitable, or in some instances even unsuitable, for the above mentioned uses.

Object of the present invention is therefore to provide a simple and economical process for preparing finely divided nickel powders which shall be free of the drawbacks of the prior art.

According to the present invention, finely divided metallic nickel powder, with spheroidal form and having dimensions lower than 1 micron, is obtained by suspending bis-acrylonitrile-nickel in methanol, and thereupon heating the resulting suspension at temperatures ranging from 100 to 200C, preferably from 150 to 180C, up to the complete decomposition.

The pyrolysis is carried out in a reactor having vitrified walls; the bis-acrylonitrile-nickel is suspended in methanol, inert towards the complex and wherein the complex is insoluble and brought to the determined temperature with stirring.

The concentration of the complex ranges from 1 to 20 percent, and preferably from 5 to 10 percent. The decomposition of the complex starts at about 110C and is carried out in a short time, at temperatures higher than 120C; the decomposition is practically ended when the suspension has become black and no longer shows red particles of bis-acrylonitrile-nickel.

The metallic nickel thus obtained is pyrophoric and may retain up to 15 percent of organic impurities. The purification is carried out by introducing hydrogen 10-100 atm) into the autoclave or other reaction vessel at the reaction temperature, and hydrogenating the organic impurities the percentage of which is thereby lowered to 3-4 percent.

EXAMPLE 15 g of bis-acrylonitrile-nickel* (*Bis-acrylonitrilenickel, (Cl-l =CH-CN) Ni, was prepared from nickelcarbonyl and acrylonitrile according to the method described by G.N. Schrauzer in J.Am.Chem. Soc., 81(1959), 5310-12.) were suspended in 400 cc of methanol and transferred, in N stream, into a 3.3 liter autoclave having enameled walls, and provided with a blade stirrer and heated by an oil jacket.

The temperature was raised to 160C over a period of two hours, whereupon hydrogen at 40 atm. was charged into the auto-clave and the stirring was continued at 160C for 2 hours. The autoclave was cooled to ambient temperature by maintaining always the mixture under stirring, then methanol and propylamine (formed by hydrogenation of acrylonitrile) were decanted.

The nickel thus obtained was washed 3 times with methanol and dried under vacuum. The nickel powder obtained in this manner was pyrophoric; it contained 3 percent ofC. 0.5 percent of H and 0.6 percent of N.

Granulometric analysis showed that 94 percent of the granules had a diameter ranging from 32 to 97 nanometers (milli-mi crons) and that 64.7 percent of the particles came within the limited zone of 57 nanometers i 20 percent (from 46 to 68 nanometers). The shape of the granules was spheroidal.

What is claimed is:

l. A process for preparing finely divided metallic nickel powder, with spheroidal form, having dimensions lower than 1 micron, wherein bis-acrylonitrilenickel is suspended in methanol, and the suspension is heated under hydrogen pressure at temperatures between 100 and 200C, up to the complete decomposition.

2. A process as defined in claim 1, wherein the temperatures are in the range 180C.

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US1138201 *Apr 24, 1912May 4, 1915Carleton EllisHydrogenating unsaturated organic material.
US3573292 *Dec 15, 1967Mar 30, 1971Studiengesellschaft Kohle MbhNovel oxygen complexes and process for the production thereof
Non-Patent Citations
Reference
1 *G. N. Schrauzer, J. Am. Chem. Soc., 81(1959), 5310 5312
Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3850612 *Sep 19, 1973Nov 26, 1974Montedison SpaProcess for preparing finely particled nickel powders having a spheroidal form
US5782954 *Jun 7, 1995Jul 21, 1998Hoeganaes CorporationIron-based metallurgical compositions containing flow agents and methods for using same
US6033624 *Sep 25, 1996Mar 7, 2000The University Of ConneticutMethods for the manufacturing of nanostructured metals, metal carbides, and metal alloys
US6316100Feb 24, 1998Nov 13, 2001Superior Micropowders LlcNickel powders, methods for producing powders and devices fabricated from same
US6406513 *Feb 2, 2001Jun 18, 2002Mitsui Mining And Smelting Co., Ltd.Nickel powder and conductive paste
US7004994Feb 9, 2004Feb 28, 2006Cabot CorporationMethod for making a film from silver-containing particles
US7083747Nov 1, 2004Aug 1, 2006Cabot CorporationAerosol method and apparatus, coated particulate products, and electronic devices made therefrom
US7087198Nov 16, 2004Aug 8, 2006Cabot CorporationAerosol method and apparatus, particulate products, and electronic devices made therefrom
US7097686Nov 9, 2001Aug 29, 2006Cabot CorporationGenerating an aerosol including a liquid comprising a nickel precursor and a reducing agent and moving the droplets through a heating zone by means of a carrier gas to form nickel particles having small particle size, narrow size distribution, spherical morphology and high crystallinity; pyrometallurgy
US7354471Sep 24, 2004Apr 8, 2008Cabot CorporationIn a flowing aerosol stream, preparing silver-containing particles, then coating with a material other than silver by vapor deposition; monodisperse silver particles confined in metal or ceramic coatings, with various uses in electronics and electrochemical cells
US7384447Nov 1, 2004Jun 10, 2008Cabot CorporationGenerating an aerosol including a nickel metal precursor and moving the droplets through a heating zone to form nickel particles; while in the aerosol stream forming a coating on the particles, the coating comprising a material is different than the nickel-containing material; flat panel displays
Classifications
U.S. Classification75/362, 75/953, 75/717
International ClassificationC22B23/00, B22F9/30
Cooperative ClassificationY10S75/953, B22F9/30
European ClassificationB22F9/30