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Browse by: INVENTOR PATENT HOLDER PATENT NUMBER DATE
 
 
Inventor:
Sakuth; Michael
Address:
Marl, DE
No. of patents:
5
Patents:












Patent Number Title Of Patent Date Issued
6881700 Dealuminized catalyst carrier, method of production, and method for hydrating C2 or C3 olefins w April 19, 2005
A catalyst support comprising silicates is described. This catalyst support has a lower aluminum content than naturally occurring sheet silicates and can be used in the hydration of C.sub.2 and C.sub.3 olefins to produce C.sub.2 and C.sub.3 alcohols. A method for the production of the ca
6881699 Method for producing a dealuminized catalyst support April 19, 2005
What is claimed is a dealuminated catalyst carrier, a process for producing a catalyst carrier with reduced aluminum content based on naturally occurring lattice-layer silicates, such as, for example, montmorillonite, as well as a process for the hydration reaction of C.sub.2 - or C.sub.
6841704 Process for preparing cumene which is used in the preparation of phenol January 11, 2005
Disclosed is a method for the preparation of cumene by reacting isopropanol or a mixture of isopropanol and propene with benzene in the presence of a .beta.-zeolite catalyst having a SiO.sub.2 /Al.sub.2 O.sub.3 molar ratio greater than 10:1 that can be integrated in a process for prepari
6552236 Process for the cleavage of alkyl tert-alkyl ethers into isoolefins and alkanols over acid catal April 22, 2003
Alkyl tert-alkyl ethers are cleaved into the corresponding isoolefins and alkanols by a process comprising acid-catalyzed reactive distilling an alkyl tert-alkyl ether fed into the reaction zone of a reactive distillation apparatus as an azeotrope of the alkyl tert-alkyl ether and th
5849971 Process for cracking tertiary butyl alcohol in a reaction distillation column December 15, 1998
The present invention is directed to a process for the acid-catalyzed cracking of tertiary butyl alcohol in a reaction distillation column. The advantage of the process of the present invention compared with conventional processes is that the two-phase, liquid-liquid region of the te










 
 
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