Patents by Inventor Holger Hackner

Holger Hackner has filed for patents to protect the following inventions. This listing includes patent applications that are pending as well as patents that have already been granted by the United States Patent and Trademark Office (USPTO).

  • Patent number: 7566679
    Abstract: The invention relates to a homogeneous catalyst for the production of linear alpha-olefins by oligomerisation of ethylene, consisting of a zirconium salt of organic acids and a cocatalyst which consists of alkylaluminiums and/or aluminium chloride. The activity of the catalyst, system may sometimes be raised substantially by adjusting the molar ratio of chlorine to aluminium in the cocatalyst within the range between 1.0 and 1.5. The economic viability of the production process and product purity are improved.
    Type: Grant
    Filed: July 7, 2005
    Date of Patent: July 28, 2009
    Assignees: Saudi Basic Industries Corporation, Linde AG
    Inventors: Heinz Bölt, Peter Fritz, Holger Hackner, Atieh Abu-Raqabah, Mohammed Zahoor, Fuad Mosa
  • Publication number: 20080176738
    Abstract: The invention relates to a homogeneous catalyst for the production of linear alpha-olefins by oligomerisation of ethylene, consisting of a zirconium salt of organic acids and a cocatalyst which consists of alkylaluminiums and/or aluminium chloride. The activity of the catalyst, system may sometimes be raised substantially by adjusting the molar ratio of chlorine to aluminium in the cocatalyst within the range between 1.0 and 1.5. The economic viability of the production process and product purity are improved.
    Type: Application
    Filed: July 7, 2005
    Publication date: July 24, 2008
    Inventors: Heinz Bolt, Peter Fritz, Holger Hackner, Atieh Abu-Raqabah, Mohammed Zahoor, Fuad Mosa
  • Patent number: 5804689
    Abstract: For recovering acetylene from hydrocarbons, the hydrocarbons are thermally cracked in the presence of CO.sub.2 as a diluent gas. Suitable for thermal cracking for acetylene generation is a ratio, by weight, of CO.sub.2 to hydrocarbon, of between 3:1 and 1:3, and preferably between 2:1 and 1:2. It is preferred for the CO.sub.2 to be mixed with the hydrocarbons before thermal cracking which is thereafter conducted at average reaction temperatures of between 800.degree. and 1200.degree. C., preferably between 900.degree. and 1100.degree. C. An average residence time of between 5 and 500 milliseconds (ms) of the hydrocarbons during thermal cracking has proven to be effective. As the hydrocarbon feedstock for the thermal cracking, basically C.sub.2+ alkanes, especially ethane, propane and/or butane, can be used advantageously. After the cracked gas is cooled, higher alkynes are removed from the cracked gas, then the acetylene is separated preferably by scrubbing with an absorption agent selective for acetylene.
    Type: Grant
    Filed: January 30, 1996
    Date of Patent: September 8, 1998
    Assignee: Linde Aktiengesellschaft
    Inventors: Nicole Schodel, Eberhard Lassmann, Holger Hackner