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Browse by: INVENTOR PATENT HOLDER PATENT NUMBER DATE
 
 
Inventor:
Wulff-Doring; Joachim
Address:
Frankenthal, DE
No. of patents:
34
Patents:




Patent Number Title Of Patent Date Issued
7553916 Loop reactor with varying diameter for olefin polymerization June 30, 2009
Process for polymerizing at least one olefinic monomer in a loop reactor at from 20 to 150.degree. C., but below the melting point of the polymer to be formed, and a pressure of from 5 to 100 bar, where the polymer formed is present in a suspension in a liquid or supercritical suspension
7517938 Loop reactor with varying diameter for olefin polymerization April 14, 2009
Process for polymerizing at least one olefinic monomer selected from ethylene, propylene and 1-butene in a loop reactor in the presence of a polymerization catalyst at from 20 to 150.degree. C., but below the melting point of a polymer to be formed, and a pressure of from 43 to 80 ba
7348384 Supported, titanized chromium catalyst and its use for preparing homopolymers and copolymers of March 25, 2008
Novel supported, titanized chromium catalysts for the homopolymerization of ethylene and the copolymerization of ethylene with .alpha.-olefins, a process for preparing them and to their use for the polymerization of olefins.
7172989 Catalytic hydrogenation over rhenium-containing catalysts supported on activated carbon February 6, 2007
In a process for preparing alcohols by catalytic hydrogenation of carbonyl compounds over a catalyst comprising rhenium on activated carbon, the catalyst used comprises rhenium (calculated as metal) in a weight ratio to the activated carbon of from 0.0001 to 0.5, platinum (calculated as
7094724 Catalytic solid supported on calcined hydrotalcite for olefinic polymerisation August 22, 2006
Catalyst solid for olefin polymerization comprising A) at least one calcined hydrotalcite and B) at least one organic transition metal compound, and also a catalyst system comprising the catalyst solid, the use of the catalyst solid for the polymerization or copolymerization of olefi
7084312 Catalyst and method for hydrogenating carbonyl compounds August 1, 2006
A process for the hydrogenation of an organic compound containing at least one carbonyl group comprises bringing the organic compound in the presence of hydrogen into contact with a shaped body which can be produced by a process in which (i) an oxidic material comprising copper oxi
7019089 Suspended chrome catalyst containing titanium and the use thereof for producing ethylene homopol March 28, 2006
Novel supported, titanized chromium catalysts can be used for the homopolymerization of ethylene and the copolymerization of ethylene with .alpha.-olefins.
6924248 Catalyst system for carrying out olefin polymerization comprising a calcined hydro-talcite servi August 2, 2005
Catalyst system for olefin polymerization comprising A) at least one calcined hydrotalcite, B) at least one organic transition metal compound, C) optionally one or more cation-forming compounds and D) at least one organic magnesium compound.
6906228 Method for catalytic hydrogenation on rhenium-containing active carbon carrier catalysts June 14, 2005
In a process for preparing alcohols by catalytic hydrogenation of carbonyl compounds over a catalyst comprising rhenium on activated carbon, the catalyst used comprises rhenium (calculated as metal) in a weight ratio to the activated carbon of from 0.0001 to 0.5, platinum (calculated as
6864208 Method for production of a solid catalyst for olefin polymerization March 8, 2005
A catalyst solid for olefin polymerization comprising A) at least one magnesium halide, B) at least one metallocene complex and C) at least one compound capable of forming metallocenium ions, is prepared by i) firstly preparing finely divided support particles consisting of the ma
6765118 Method for the production of alcohols on rhenium-containing activated charcoal supported catalys July 20, 2004
In a process for the preparation of alcohols by catalytic hydrogenation of carbonyl compounds, the catalyst used is 0.01 to 50% by weight of rhenium and 0 to 20% by weight, in each case based on the total weight of the catalyst, of at least one further metal chosen from Zn, Cu, Ag, Au, N
6525222 Process for preparing amines February 25, 2003
Amines are prepared by reacting aldehydes or ketones at elevated temperature under elevated pressure with nitrogen compounds selected from the group of ammonia, primary and secondary amines, and with hydrogen in the presence of a catalyst, wherein the catalytically active mass of the
6429339 Method for producing cyclopentanone August 6, 2002
A process for preparing cyclopentanone by reacting adipic esters of the formulawhere R.sub.1 and R.sub.2 are each alkyl having from 1 to 12 carbon atoms, cycloalkyl having 5 or 6 carbon atoms, aralkyl or aryl and R.sub.2 may additionally be hydrogen, in the presence of oxidic catalysts c
6417353 Preparing amines July 9, 2002
Amines are prepared by reacting aldehydes or ketones at elevated temperature under elevated pressure with nitrogen compounds selected from the group of ammonia, primary and secondary amines, and with hydrogen in the presence of a catalyst containingcopper, wherein the catalytically activ
6284932 Method for producing alcohols containing cycloaliphatic groups September 4, 2001
In a process for preparing alcohols containing cycloaliphatic groups by hydrogenation of carboxylic acids containing aromatic nuclei, or anhydrides or esters thereof, in the presence of a catalyst, the hydrogenation is carried out in one stage, and the catalyst contains at least one
6262317 Process for preparing 1,4-butanediol by catalytic hydrogenation of 1,4-butinediol July 17, 2001
A process for preparing 1,4-butanediol by continuous catalytic hydrogenation of 1,4-butynediol comprises reacting 1,4-butynediol with hydrogen in the liquid continuous phase in the presence of a heterogeneous hydrogenation catalyst at from 20 to 300.degree. C., a pressure of from 1 t
6204417 Method for producing aliphatic alcohols March 20, 2001
In a process for preparing aliphatic alcohols by hydrogenating aliphatic carboxylic acids or anhydrides or esters thereof or lactones in the presence of a catalyst comprising Pt and Re, in the form of the metal or an oxide in each case, the catalyst further comprises at least one further
6162928 Preparation of pyrroles December 19, 2000
A process for preparing pyrroles of the formula I: ##STR1## where R.sub.1, R.sup.2, R.sup.3 and R.sup.4 are identical or different and are hydrogen atoms, alkyl groups having from 1 to 12 carbon atoms or cycloalkyl groups having from 3 to 12 carbon atoms, by dehydrogenation of py
6140545 Preparation of alcohols October 31, 2000
In a process for preparing alcohols by gas phase hydrogenation of carboxylic acids or esters thereof at elevated temperature and elevated pressure in the presence of catalysts consisting of or comprising, as hydrogenating components, oxides of main group VI and/or subgroup IV, the hy
6057442 Preparation of amines May 2, 2000
Amines are prepared from primary or secondary alcohols and nitrogen compounds selected from the group of ammonia, primary and secondary amines, at from 80 to 250.degree. C. under pressures from 0.1 to 40 MPa with hydrogen in the presence of a catalyst comprising zirconium, copper and
6046359 Catalysts for the amination of alkylene oxides, alcohols, aldehydes and ketones April 4, 2000
A catalyst comprises, based on the total weight of the catalyst,0.1-6% by weight of cobalt, nickel or a mixture thereof,0.001-25% by weight of ruthenium,0-10% by weight of copper and0-5% by weight of promoterson a porous metal oxide carrier.It preferably comprises 0.1-3% by weight of cobalt and 0.1-
6034029 Monoclinic zirconium dioxide having a large surface area March 7, 2000
Zirconium dioxide which is monoclinic to at least 80% by weight and has a BET surface area of at least 100 m.sup.2 /g is prepared by admixing aqueous zirconium salt solutions with ammonia, drying and calcining the precipitation product, aging the precipitation product, prior to drying,
6020501 Process for preparing phthalides February 1, 2000
The disclosure is a process for preparing a phthalide of the general formula I ##STR1## where R.sup.1, R.sup.2, R.sup.3 and R.sup.4 are each independently of the others hydrogen, C.sub.1 -C.sub.4 -alkyl or C.sub.1 -C.sub.4 -alkoxy, by hydrogenation of a phthalic anhydride of the
6013844 Preparation of catechol monoethers and catechols January 11, 2000
A process for preparing catechol monoethers or catechols of the formula Ia or Ib ##STR1## where R.sup.1 and R.sup.2 are, independently of one another, hydrogen or C.sub.1 -C.sub.8 hydrocarbon radicals, and R.sup.3 is a C.sub.1 -C.sub.8 hydrocarbon radical, which comprises a 2-hyd
5958825 Catalysts for the amination of alkylene oxides, alcohols, aldehydes and ketones September 28, 1999
A catalyst comprising, based on the total weight of the catalyst,more than 6-50% by weight of cobalt, nickel or a mixture thereof,0.001-25% by weight of ruthenium,0-10% by weight of copper and0-5% by weight of promoterson a porous metal oxide carrier can be prepared by(a) impregnating the carrier wi
5916838 Catalysts for the amination of alkylene oxides, alcohols, aldehydes and ketones June 29, 1999
A catalyst comprises, based on the total weight of the catalyst,0.1-6% by weight of cobalt, nickel or a mixture thereof,0.001-25% by weight of ruthenium,0-10% by weight of copper and0-5% by weight of promoterson a porous metal oxide carrier.It preferably comprises 0.1-3% by weight of cobalt and 0.1-
5840986 Preparation with heterogeneous catalysis of N-alkyl-substituted aminoalkynes November 24, 1998
A process for preparing N-alkyl-substituted aminoalkynes by reacting an alkyne with a carbonyl compound and an amine with heterogeneous catalysis in which an unsupported copper acetylide derived from malachite is used as the catalyst. The N-alkyl-substituted aminoalkyne have a wide varie
5831129 Preparation, with heterogeneous catalysis, of N-hydroxyalkyl-substituted aminoalkynes November 3, 1998
N-Hydroxyalkyl-substituted aminoalkynes of the formula I ##STR1## are prepared by reacting an alkyne with a 1-oxa-3-azaheterocyclo-alkane in a reaction with heterogeneous catalysis by a catalyst which comprises a compound of a metal of the first or second sub-group.
5783711 Process for the preparation of heterocyclic aldehydes July 21, 1998
Preparation of heterocyclic aldehydes I ##STR1## (A, B=optionally substituted methylene groups; m, n=1 to 5; m+n>2), by hydrogenation of carboxylic acids IIa ##STR2## or one of their esters IIb derived from a C.sub.1 -C.sub.10 alcohol, at a temperature of from 200.degree.
5763676 Preparation of aromatic aldehydes June 9, 1998
Aromatic aldehydes are prepared by catalytically reacting aromatic carboxylic acids or their esters with hydrogen in the gas phase at from 200.degree. to 450.degree. C. and from 0.1 to 20 bar in the presence of a zirconium dioxide/lanthanide catalyst having a high BET surface area of
5733838 Process for the production of a hydrogenation catalyst March 31, 1998
A hydrogenation catalyst based on an alloy of aluminum and of a transition metal is prepared by preparing a kneaded material from the alloy and an assistant, converting the kneaded material into moldings, calcining the moldings and treating the calcined moldings with an alkali metal
5679869 Preparation of aldehydes October 21, 1997
A process for preparing aldehydes of the general formula I ##STR1## where R.sup.1, R.sup.2 and R.sup.3 are each hydrogen, C.sub.1 -C.sub.6 -alkyl, C.sub.3 -C.sub.8 -cycloalkyl, aryl, C.sub.7 -C.sub.12 -alkylphenyl, C.sub.7 -C.sub.12 -phenylalkyl and R.sup.1 and R.sup.2 are joined
5663438 Preparation of cyclic amines September 2, 1997
A process for the preparation of a phenyl amine which may be substituted by alkyl or cycloalkyl in which the corresponding cyolohexylamine is reduced at temperatures of 150.degree. to 300.degree. C. and pressures of 0.01 to 50 bar in the presence of a heterogeneous dehydrogenation cataly
5508465 Preparation of aliphatic alpha, omega-aminonitriles in the gas phase April 16, 1996
Aliphatic alpha,omega-aminonitriles are prepared by partial hydrogenation of aliphatic alpha,omega-dinitriles at elevated temperatures in the presence of a catalyst in the gas phase by a process which comprises carrying out the hydrogenation with a catalyst based on at least one metal


 
 
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