US1628190A - Method of producing finely-divided nickel - Google Patents

Method of producing finely-divided nickel Download PDF

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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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nickel
aluminum
silicon
alloy
alloying
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US109169A
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Raney Murray
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22FWORKING METALLIC POWDER; MANUFACTURE OF ARTICLES FROM METALLIC POWDER; MAKING METALLIC POWDER; APPARATUS OR DEVICES SPECIALLY ADAPTED FOR METALLIC POWDER
    • B22F9/00Making metallic powder or suspensions thereof
    • B22F9/16Making metallic powder or suspensions thereof using chemical processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J25/00Catalysts of the Raney type
    • B01J25/02Raney nickel
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11CFATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C3/00Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
    • C11C3/12Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by hydrogenation
    • C11C3/123Fats, 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.
US109169A 1926-05-14 1926-05-14 Method of producing finely-divided nickel Expired - Lifetime US1628190A (en)

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Cited By (67)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
EP2085385A1 (en) 2008-02-01 2009-08-05 Evonik Degussa GmbH Method of manufacturing 4-Amino-2,2,6,6-tetramethylpiperidin
DE202010007837U1 (en) 2010-06-10 2010-10-07 Hasenpusch, Wolfgang, Prof. Dr. Device in the production of Raney metals
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
WO2012174429A1 (en) 2011-06-17 2012-12-20 CHEMTEX ITALIA, S.p.A Lignin conversion process
WO2013019440A1 (en) 2011-07-29 2013-02-07 Eastman Chemical Company Integrated process for the preparation of 1,4-cyclohexanedimethanol from terephtalic acid
WO2013019439A1 (en) 2011-07-29 2013-02-07 Eastman Chemical Company Process for the preparation of 1,4-cyclohexanedimethanol
WO2013019442A1 (en) 2011-07-29 2013-02-07 Eastman Chemical Company Process for the preparation of 1,3-cyclohexanedimethanol from isophthalic acid
WO2013019441A1 (en) 2011-07-29 2013-02-07 Eastman Chemical Company Process for the preparation of 1,4-cyclohexanedimethanol from terephthalic acid
WO2013124458A2 (en) 2012-02-24 2013-08-29 Chemtex Italia S.P.A. Continuous process for conversion of lignin to useful compounds
WO2013124647A2 (en) 2012-02-24 2013-08-29 Teer Coatings Limited High surface area (hsa) coatings and method for forming the same
US20130225872A1 (en) * 2012-02-24 2013-08-29 Chemtex Italia, S.p.A. Continuous process for conversion of lignin to useful compounds
WO2014053344A1 (en) 2012-10-04 2014-04-10 Basf Se Method for producing phenylcyclohexane
WO2014063842A1 (en) 2012-10-28 2014-05-01 Biochemtex S.P.A. Improved process for conversion of lignin to useful compounds
WO2014063852A1 (en) 2012-10-28 2014-05-01 Biochemtex S.P.A. Continuous process for conversion of lignin to useful compounds
US8735635B2 (en) 2009-02-25 2014-05-27 W. R. Grace & Co.-Conn. Process for making 1, 2-propane diol from hydrogenation of glycerol
WO2014108238A1 (en) 2013-01-13 2014-07-17 Biochemtex S.P.A. Continuous process for conversion of lignin to useful compounds
WO2014152472A1 (en) 2013-03-15 2014-09-25 W. R. Grace & Co.-Conn. Process for the selective production of propanols by hydrogenation of glycerol
WO2015062735A2 (en) 2013-10-31 2015-05-07 Biochemtex S.P.A. Continuous lignin conversion process
WO2017184710A1 (en) 2016-04-22 2017-10-26 Invista North America S.A R.L. Heterogeneous catalyst process and nickel catalyst
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US20190185447A1 (en) * 2012-10-12 2019-06-20 Exelixis, Inc. Novel process for making compounds for use in the treatment of cancer
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Cited By (92)

* Cited by examiner, † Cited by third party
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
US4728363A (en) * 1985-12-02 1988-03-01 Olin Corporation Acicular magnetic particles
US4657583A (en) * 1985-12-02 1987-04-14 Olin Corporation Method of producing ferromagnetic particles
US4828613A (en) * 1986-09-01 1989-05-09 Mitsubishi Kinzoku Kabushiki Kaisha Powdery raw material for manufacturing anodes of fuel cells
US4826799A (en) * 1988-04-14 1989-05-02 W. R. Grace & Co.-Conn. Shaped catalyst and process for making it
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
US6995107B2 (en) 1995-11-08 2006-02-07 Towa Chemical Industry Co., Ltd. Raney catalyst, process for producing it and process for producing a sugar-alcohol using the same
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
US20050153837A1 (en) * 1995-11-08 2005-07-14 Towa Chemical Industry Co., Ltd. Raney catalyst, process for producing it and process for producing a sugar-alcohol using the same
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
EP2085385A1 (en) 2008-02-01 2009-08-05 Evonik Degussa GmbH Method of manufacturing 4-Amino-2,2,6,6-tetramethylpiperidin
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
DE202010007837U1 (en) 2010-06-10 2010-10-07 Hasenpusch, Wolfgang, Prof. Dr. Device in the production of Raney metals
WO2012174429A1 (en) 2011-06-17 2012-12-20 CHEMTEX ITALIA, S.p.A Lignin conversion process
WO2013019442A1 (en) 2011-07-29 2013-02-07 Eastman Chemical Company Process for the preparation of 1,3-cyclohexanedimethanol from isophthalic acid
WO2013019440A1 (en) 2011-07-29 2013-02-07 Eastman Chemical Company Integrated process for the preparation of 1,4-cyclohexanedimethanol from terephtalic acid
WO2013019441A1 (en) 2011-07-29 2013-02-07 Eastman Chemical Company Process for the preparation of 1,4-cyclohexanedimethanol from terephthalic acid
US8410317B2 (en) 2011-07-29 2013-04-02 Eastman Chemical Company Process for the preparation of 1,4-cyclohexanedimethanol
US8410318B2 (en) 2011-07-29 2013-04-02 Eastman Chemical Company Process for the preparation of 1,4-cyclohexanedimethanol from terephthalic acid
WO2013019439A1 (en) 2011-07-29 2013-02-07 Eastman Chemical Company Process for the preparation of 1,4-cyclohexanedimethanol
US8877984B2 (en) 2011-07-29 2014-11-04 Eastman Chemical Company Process for the preparation of 1,3-cyclohexanedimethanol from isophthalic acid
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