US1628190A - Method of producing finely-divided nickel - Google Patents
Method of producing finely-divided nickel Download PDFInfo
- Publication number
- US1628190A US1628190A US109169A US10916926A US1628190A US 1628190 A US1628190 A US 1628190A US 109169 A US109169 A US 109169A US 10916926 A US10916926 A US 10916926A US 1628190 A US1628190 A US 1628190A
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- US
- United States
- Prior art keywords
- nickel
- aluminum
- silicon
- alloy
- alloying
- 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.)
- Expired - Lifetime
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22F—WORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
- B22F9/00—Making metallic powder or suspensions thereof
- B22F9/16—Making metallic powder or suspensions thereof using chemical processes
-
- 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
- B01J25/00—Catalysts of the Raney type
- B01J25/02—Raney nickel
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/12—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by hydrogenation
- C11C3/123—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by hydrogenation using catalysts based principally on nickel or derivates
Definitions
- Thi invention relates to a method of the invention is not to be restricted to the preparing catalytic or finely divided mapro rtions given.
- T e solvent may be of any desired
- the principal object of the invention is strength, dependent upon the rapidity with the production of metallic nickel in a catawhic it is desired to remove the aluminum, co lytic state such as may be used in the hydroor the aluminum and silicon.
- co lytic state such as may be used in the hydroor the aluminum and silicon.
- the invention contemplates the drogen is liberated, and this may be saved alloying of metallic nickel with metals such and used for other purposes, or not, as found as silicon and aluminum in various proporconvenient and expedient.
- the ,steps pursued in the treatment of the I have gotten eflicient results in the nickel nickel are as follows and alumlnum compound between the ranges 75
- the proper proportions of nickel, alumof from 10% to 85% nickel, and from 90% inum and silicon are either melted separateto 15% aluminum respectively. ly, or together, and if the former, poured
- the aluminum nickel alloy possesses chartogether in a suitable vessel. If this proacteristics which are not possessed by an cedure is to be used, great care should be alloy containing these same substances and so exercised, as the alloy is formed in an exosilicon. That is, the nickel aluminum alloy thermic reaction.
- the melt may be made in a graphite 0111- 200 mesh, or it may be broken in pieces the proficient in any desired type of furnace or fire, lz Peas 01 smaller- In either condicare bein used to prevent contamination 1011 the alloy may be treated with caustic of the me t by impurities from th fire, soda or the aluminum removed with the After the melt has fused and been thoruse of some other solvent. In case the larger oughly coinniingled, it is allowed to cool and pieces are used, the nickel is left in a more is then pulverized in any desired apparatus.
- Thenickel thus produced is ready for use 1.
- a method of preparing a catalytic maas a catalyzer. terial which includes the step of alloying the I have found that catalytic ni k l may be same with aluminum and dissolving the produced in the above manner by alloying aluminum from the resultant alloy, whereby that metal with either aluminum or with the the catalytic material remains in finely combination of silicon and aluminum, the divided condition. operation for reaching the desired end being 2.
- a process of preparing a catalyzer .the same.
- a method of preparing a catalytic material which includes the step of alloying 50% nickel, 40% silicon, and 10% aluminum, and dissolving the silicon and aluminum from the resultant alloy.
- a method of preparing finel divided nickel which includes the step of alloying nickel with aluminum and dissolving the aluminum from the resulting alloy with a. solvent which will not dissolve the nickel and drying the resultant finely divided nickel.
- a method of preparing finely divided nickel which includes the step of alloying nickel with aluminum and silicon dissolving the aluminum and silicon from the resultant alloy with a solvent which will not dissolve nickel and drying the finely divided product.
- a method of preparing finely divided nickel which includes the step of alloying 50% nickel, 40% silicon and 10% aluminum and dissolving the silicon and aluminum from the resultant? alloy and separating the ⁇ inelyl divided nickel from the supernatant iqui In testimony whereof, I afiix my signature.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Materials Engineering (AREA)
- Catalysts (AREA)
- Manufacture Of Metal Powder And Suspensions Thereof (AREA)
Description
15 divided state.
Patented May 10, 1927.
UNITED STATES PATENT OFFICE.
IUD-RAY HEY, OF CHAT'IANOOGA, TENNESSEE.
IE'IKOD OI PRODUCING FINEIiY-DIVIDED NICKEL.
Io Drawing. Application filed Kay 14, 1926. Serial No. 100,109.
Thi invention relates to a method of the invention is not to be restricted to the preparing catalytic or finely divided mapro rtions given. terial. T e solvent may be of any desired The principal object of the invention is strength, dependent upon the rapidity with the production of metallic nickel in a catawhic it is desired to remove the aluminum, co lytic state such as may be used in the hydroor the aluminum and silicon. In the disgenation of oils, fats, waxes and thelike. solving action a considerable amount of hy- To this end the invention contemplates the drogen is liberated, and this may be saved alloying of metallic nickel with metals such and used for other purposes, or not, as found as silicon and aluminum in various proporconvenient and expedient. 65 tions, and then dissolving the aluminum After having dissolved out the aluminum and silicon from the alloy by means of a or the aluminum and silicon the resulting solvent which will not attack the nickel, finely divided nickel may be dried at atwhereupon the nickel remains ina finely mospheric temperature or in any other way exposed to the air, as a result of which the 70 In this condition the nickel may be exnickel does not have catalytic properties, tremely catalytic. these properties apparentbut this substance is in this form suitable ly being intensified by t e treatment. for many purposes. a I
The ,steps pursued in the treatment of the I have gotten eflicient results in the nickel nickel are as follows and alumlnum compound between the ranges 75 The proper proportions of nickel, alumof from 10% to 85% nickel, and from 90% inum and silicon are either melted separateto 15% aluminum respectively. ly, or together, and if the former, poured The aluminum nickel alloy possesses chartogether in a suitable vessel. If this proacteristics which are not possessed by an cedure is to be used, great care should be alloy containing these same substances and so exercised, as the alloy is formed in an exosilicon. That is, the nickel aluminum alloy thermic reaction. may be either very finely pulverized, say to The melt may be made in a graphite 0111- 200 mesh, or it may be broken in pieces the cible in any desired type of furnace or fire, lz Peas 01 smaller- In either condicare bein used to prevent contamination 1011 the alloy may be treated with caustic of the me t by impurities from th fire, soda or the aluminum removed with the After the melt has fused and been thoruse of some other solvent. In case the larger oughly coinniingled, it is allowed to cool and pieces are used, the nickel is left in a more is then pulverized in any desired apparatus. or less spongy and porous state, somewhat In its ground form it is .then subj ted to slmilar to a cinder, and for certain classes the action of a solvent such as causti soda, of work is is necessary and desirable to have or th lik whi h will di solve ll f th the catalyzer in this condition. I find this alloyed material with the exception of the Characteristic peculiar to the aluminum nickel. After this treatment the subnatent ni kel alloy. fluid is' decanted and the residue, consisting Having thus described my invention, what of finely divided nickel thoroughl washed. 1 lenn is:-
Thenickel thus produced is ready for use 1. A method of preparing a catalytic maas a catalyzer. terial which includes the step of alloying the I have found that catalytic ni k l may be same with aluminum and dissolving the produced in the above manner by alloying aluminum from the resultant alloy, whereby that metal with either aluminum or with the the catalytic material remains in finely combination of silicon and aluminum, the divided condition. operation for reaching the desired end being 2. A process of preparing a catalyzer .the same. which includes the step of alloying nickel 5 I have found a satisfactory proportion of and aluminum, and treating the alloy with 105 the aluminum nickel allo to be aluma solvent which will dissolve the aluminum inum and 50% nickel, and in the three-metal but not the nickel. alloy, 50% nickel, 40% silicon, and 10% 3. A process of preparing a catalyzer aluminum, although obviously I do not wish which includes the mp of alloying nickel to be limited to the exact proportions, as with aluminum and silicon, and dissolving 110 the aluminum and silicon from the resultant alloy.
4. A method of preparing a catalytic material which includes the step of alloying 50% nickel, 40% silicon, and 10% aluminum, and dissolving the silicon and aluminum from the resultant alloy.
5. A method of preparing finel divided nickel which includes the step of alloying nickel with aluminum and dissolving the aluminum from the resulting alloy with a. solvent which will not dissolve the nickel and drying the resultant finely divided nickel. v
6. A method of preparing finely divided nickel which includes the step of alloying nickel with aluminum and silicon dissolving the aluminum and silicon from the resultant alloy with a solvent which will not dissolve nickel and drying the finely divided product. 7. A method of preparing finely divided nickel which includes the step of alloying 50% nickel, 40% silicon and 10% aluminum and dissolving the silicon and aluminum from the resultant? alloy and separating the {inelyl divided nickel from the supernatant iqui In testimony whereof, I afiix my signature.
MURRAY RANEY.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US109169A US1628190A (en) | 1926-05-14 | 1926-05-14 | Method of producing finely-divided nickel |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US109169A US1628190A (en) | 1926-05-14 | 1926-05-14 | Method of producing finely-divided nickel |
Publications (1)
Publication Number | Publication Date |
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US1628190A true US1628190A (en) | 1927-05-10 |
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Family Applications (1)
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US109169A Expired - Lifetime US1628190A (en) | 1926-05-14 | 1926-05-14 | Method of producing finely-divided nickel |
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Cited By (67)
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US2447980A (en) * | 1945-01-29 | 1948-08-24 | Mallory & Co Inc P R | Method of making porous bearing surfaces |
US2450339A (en) * | 1943-09-17 | 1948-09-28 | Mallory & Co Inc P R | Method of making porous metal filters |
US2461396A (en) * | 1945-07-25 | 1949-02-08 | Raney Murray | Method of producing finely divided metals |
US2462045A (en) * | 1942-04-04 | 1949-02-15 | Wulff John | Method of producing filters |
US2475718A (en) * | 1946-08-12 | 1949-07-12 | Schering Corp | Process for the hydrogenation of naphthalene compounds |
US2502348A (en) * | 1944-11-20 | 1950-03-28 | Rhone Poulenc Sa | Catalysts |
US2583619A (en) * | 1944-03-15 | 1952-01-29 | Standard Oil Co | Preparation of a raney catalyst surface |
US2608469A (en) * | 1947-06-19 | 1952-08-26 | Indiana Steel Products Co | Continuous process for leaching an iron-aluminum alloy |
US2610212A (en) * | 1950-04-24 | 1952-09-09 | Gen Mills Inc | Synthesis of amino acids |
US2750271A (en) * | 1952-03-19 | 1956-06-12 | Electro Chimie Metal | Process of making pulverulent metallic titanium |
US2766152A (en) * | 1951-11-16 | 1956-10-09 | Sylvania Electric Prod | Method of producing germanium crystals |
US2903438A (en) * | 1955-02-07 | 1959-09-08 | Celanese Corp | Treatment of raney metal suspensions |
US2946677A (en) * | 1958-11-24 | 1960-07-26 | Oregon Metallurgical Corp | Treatment of alloys containing iron group metals |
US2948687A (en) * | 1955-12-13 | 1960-08-09 | Gen Electric | Hydrogenation catalyst |
US2977327A (en) * | 1958-09-26 | 1961-03-28 | Raney Catalyst Company Inc | Process of producing nickel catalysts |
DE1197066B (en) * | 1961-01-27 | 1965-07-22 | Varta Ag | Double skeleton catalyst electrode and process for its manufacture |
US3525702A (en) * | 1966-02-05 | 1970-08-25 | Siemens Ag | Method of increasing the activity and stability of raney-type catalysts |
US3544485A (en) * | 1967-10-16 | 1970-12-01 | Toray Industries | Method of activating catalytic alloys |
US3691103A (en) * | 1969-03-25 | 1972-09-12 | Magyar Tudomanyos Akademia | Process for the preparation of a non-pyrophoric nickel skeleton catalyst |
US4247722A (en) * | 1980-03-05 | 1981-01-27 | E. I. Du Pont De Nemours And Company | Hydrogenation of butadienepolyperoxide with activated phase-pure NiAl3 |
US4650876A (en) * | 1984-08-17 | 1987-03-17 | Stauffer Chemical Company | Hydrogenation of substituted, unsaturated hydantoins to substituted, saturated hydantoins |
US4657583A (en) * | 1985-12-02 | 1987-04-14 | Olin Corporation | Method of producing ferromagnetic particles |
US4728363A (en) * | 1985-12-02 | 1988-03-01 | Olin Corporation | Acicular magnetic particles |
US4826799A (en) * | 1988-04-14 | 1989-05-02 | W. R. Grace & Co.-Conn. | Shaped catalyst and process for making it |
US4828613A (en) * | 1986-09-01 | 1989-05-09 | Mitsubishi Kinzoku Kabushiki Kaisha | Powdery raw material for manufacturing anodes of fuel cells |
US5574181A (en) * | 1991-12-18 | 1996-11-12 | Dsm N.V. | Process for the preparation of an aminoitrile by partial hydrogenation of a nitrile compound with two or more nitrile groups |
US6331624B1 (en) | 2000-04-05 | 2001-12-18 | E.I. Du Pont De Nemours And Company | Process for preparing 6-aminocaproamide |
US6372939B1 (en) | 2000-11-16 | 2002-04-16 | E.I. Du Pont De Nemours And Company | Production of 6-aminocaproic acid |
US6414201B1 (en) * | 1995-11-08 | 2002-07-02 | Towa Chemical Industry Co., Ltd. | Raney catalyst, process for producing it and process for producing a sugar-alcohol using the same |
US6558533B2 (en) | 2001-04-13 | 2003-05-06 | W.R. Grace & Co.-Conn | Process for sulfur removal from hydrocarbon liquids |
US20050020718A1 (en) * | 2001-09-25 | 2005-01-27 | Claudius Gosse | Plasticised polyvinyl chloride |
US6919489B1 (en) | 2004-03-03 | 2005-07-19 | Eastman Chemical Company | Process for a cyclohexanedimethanol using raney metal catalysts |
US20090146083A1 (en) * | 2000-03-23 | 2009-06-11 | Blacklight Power, Inc. | Hydrogen catalysis |
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DE202010007837U1 (en) | 2010-06-10 | 2010-10-07 | Hasenpusch, Wolfgang, Prof. Dr. | Device in the production of Raney metals |
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1926
- 1926-05-14 US US109169A patent/US1628190A/en not_active Expired - Lifetime
Cited By (92)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2462045A (en) * | 1942-04-04 | 1949-02-15 | Wulff John | Method of producing filters |
US2450339A (en) * | 1943-09-17 | 1948-09-28 | Mallory & Co Inc P R | Method of making porous metal filters |
US2583619A (en) * | 1944-03-15 | 1952-01-29 | Standard Oil Co | Preparation of a raney catalyst surface |
US2502348A (en) * | 1944-11-20 | 1950-03-28 | Rhone Poulenc Sa | Catalysts |
US2447980A (en) * | 1945-01-29 | 1948-08-24 | Mallory & Co Inc P R | Method of making porous bearing surfaces |
US2461396A (en) * | 1945-07-25 | 1949-02-08 | Raney Murray | Method of producing finely divided metals |
US2475718A (en) * | 1946-08-12 | 1949-07-12 | Schering Corp | Process for the hydrogenation of naphthalene compounds |
US2608469A (en) * | 1947-06-19 | 1952-08-26 | Indiana Steel Products Co | Continuous process for leaching an iron-aluminum alloy |
US2610212A (en) * | 1950-04-24 | 1952-09-09 | Gen Mills Inc | Synthesis of amino acids |
US2766152A (en) * | 1951-11-16 | 1956-10-09 | Sylvania Electric Prod | Method of producing germanium crystals |
US2750271A (en) * | 1952-03-19 | 1956-06-12 | Electro Chimie Metal | Process of making pulverulent metallic titanium |
US2903438A (en) * | 1955-02-07 | 1959-09-08 | Celanese Corp | Treatment of raney metal suspensions |
US2948687A (en) * | 1955-12-13 | 1960-08-09 | Gen Electric | Hydrogenation catalyst |
US2977327A (en) * | 1958-09-26 | 1961-03-28 | Raney Catalyst Company Inc | Process of producing nickel catalysts |
US2946677A (en) * | 1958-11-24 | 1960-07-26 | Oregon Metallurgical Corp | Treatment of alloys containing iron group metals |
DE1197066B (en) * | 1961-01-27 | 1965-07-22 | Varta Ag | Double skeleton catalyst electrode and process for its manufacture |
US3525702A (en) * | 1966-02-05 | 1970-08-25 | Siemens Ag | Method of increasing the activity and stability of raney-type catalysts |
US3544485A (en) * | 1967-10-16 | 1970-12-01 | Toray Industries | Method of activating catalytic alloys |
US3691103A (en) * | 1969-03-25 | 1972-09-12 | Magyar Tudomanyos Akademia | Process for the preparation of a non-pyrophoric nickel skeleton catalyst |
US4247722A (en) * | 1980-03-05 | 1981-01-27 | E. I. Du Pont De Nemours And Company | Hydrogenation of butadienepolyperoxide with activated phase-pure NiAl3 |
US4650876A (en) * | 1984-08-17 | 1987-03-17 | Stauffer Chemical Company | Hydrogenation of substituted, unsaturated hydantoins to substituted, saturated hydantoins |
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US20090146083A1 (en) * | 2000-03-23 | 2009-06-11 | Blacklight Power, Inc. | Hydrogen catalysis |
US6331624B1 (en) | 2000-04-05 | 2001-12-18 | E.I. Du Pont De Nemours And Company | Process for preparing 6-aminocaproamide |
US6372939B1 (en) | 2000-11-16 | 2002-04-16 | E.I. Du Pont De Nemours And Company | Production of 6-aminocaproic acid |
US6558533B2 (en) | 2001-04-13 | 2003-05-06 | W.R. Grace & Co.-Conn | Process for sulfur removal from hydrocarbon liquids |
US20050020718A1 (en) * | 2001-09-25 | 2005-01-27 | Claudius Gosse | Plasticised polyvinyl chloride |
US7297738B2 (en) | 2001-09-25 | 2007-11-20 | Exxonmobil Chemical Patents Inc. | Plasticized polyvinyl chloride |
US7413813B2 (en) | 2001-09-25 | 2008-08-19 | Exxonmobil Chemical Patents Inc. | Plasticised polyvinyl chloride |
US7585571B2 (en) | 2001-09-25 | 2009-09-08 | Exxonmobil Chemical Patents Inc. | Plasticised polyvinyl chloride |
US7855340B2 (en) | 2001-09-25 | 2010-12-21 | Exxonmobil Chemical Patents Inc. | Plasticised polyvinyl chloride |
US6919489B1 (en) | 2004-03-03 | 2005-07-19 | Eastman Chemical Company | Process for a cyclohexanedimethanol using raney metal catalysts |
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US8735635B2 (en) | 2009-02-25 | 2014-05-27 | W. R. Grace & Co.-Conn. | Process for making 1, 2-propane diol from hydrogenation of glycerol |
WO2010117986A1 (en) | 2009-04-07 | 2010-10-14 | E. I. Du Pont De Nemours And Company | Hydrogenation process for the preparation of tetrahydrofuran and alkylated derivatives thereof |
WO2011017510A2 (en) | 2009-08-06 | 2011-02-10 | Lubrizol Advanced Materials, Inc. | Method for synthesizing aminoalcohols |
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