The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Apr. 21, 2009

Filed:

Feb. 10, 2005
Applicants:

William Davey, Frankfurt am Main, DE;

Thomas Wurzel, Oberursel, DE;

Inventors:

William Davey, Frankfurt am Main, DE;

Thomas Wurzel, Oberursel, DE;

Assignee:

Lurgi AG, Frankfurt am Main, DE;

Attorney:
Primary Examiner:
Assistant Examiner:
Int. Cl.
CPC ...
C07C 27/14 (2006.01);
U.S. Cl.
CPC ...
Abstract

The invention relates to a method for the coproduction of methanol and ammonia from natural gas involving the following steps: 1. Natural gas (flow) , steam and oxygen are mixed with one another in a reactor A during which the natural gas is partially oxidized and additionally reformed with the aid of catalysts; 2. The gas mixture removed from reactor A is split into a flow (flow) for synthesizing methanol in a unit E and into another flow (flow) for producing hydrogen; 3. The carbon monoxide present in flow (flow) for producing hydrogen is converted into carbon dioxide inside reactor B with the aid of catalysts and intermediate cooling stages; 4. Remaining impurities such as methane, traces of carbon monoxide and argon are washed out in a cleaning unit D, and hydrogen (flows) is fed to the methanol synthesis in unit E and to the ammonia synthesis in unit F; 5. The methanol synthesis gas (flow) is converted into methanol (flow) with the aid of a catalyst, and the methanol is brought to the required level of purity by distillation; 6. The ammonia synthesis gas,(flow) is compressed in unit F and converted into ammonia (flow) with the aid of a catalyst, and the ammonia is separated from the recovered synthesis gas by partial condensation.


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