Metallgesellschaft Aktiengesellschaft

Friedrich W Moller

Heinz Jockel

Friedemann Marschner

Hans J Renner

Emil Supp

Walter Boll

Gerhard Cornelius

Hagen Krumm

Heiner Tanz

Hans Gunter Mortel

Gerd Siebert

Hans-Gunter Mortel

A process of producing a town-gas-grade fuel gas having a calorific value below 18,000 kJ/standard m.sup.3 (4,300 kcal/standard m.sup.3) by a catalytic reaction of methanol and water vapor under a pressure of 10 to 50 bars is disclosed wherein 80 to 95 percent of the mixed feedstock (methanol and water vapor) is fed in a water vapor to methanol weight ratio of 0.5 to 1.5 to a first reaction zone where it is maintained at a temperature of 300.degree. to 700.degree. C. in contact with a nickel catalyst containing 25 to 50 weight percent nickel, the remainder of the mixed feedstock being mixed with the effluent gas from the first reaction zone and together passed to a second reaction zone at a temperature of 200.degree. to 400.degree. C. and therein contacted with a copper catalyst containing 40 to 70 percent by weight copper.

Process of producing town gas from methanol

A process is described for producing carbon monoxide and hydrogen which comprises contacting methanol vapor at a temperature of 200.degree. to 500.degree. C. with an indirectly heated zinc containing catalyst while said methanol vapor is at a pressure in a range of 2 to 50 bars, whereby to obtain an effluent gas in which the components of carbon monoxide and hydrogen constitute at least 90% by volume of said gas, removing at least a part of the impurities from said effluent gas and separating said effluent gas into its carbon monoxide and hydrogen components by adsorption. The effluent gas can be separated into its carbon monoxide and hydrogen components by use of a plurality of adsorbers containing zeolite-type molecular sieve material where the zeolite is substantially permeable to hydrogen but sorbs carbon monoxide.

Process for producing carbon monoxide and hydrogen from methanol

A process for the catalytic production of gasoline hydrocarbons from synthesis gas comprising carbon oxides and hydrogen is disclosed wherein the synthesis gas is fed initially to a methanol synthesis and thereafter effluent from the methanol synthesis is converted to gasoline hydrocarbons in a gasoline synthesis stage. The invention resides in that the entire effluent from the methanol synthesis stage is fed to the gasoline synthesis stage and at least a portion of the residual gases from the gasoline synthesis stage comprising carbon oxides, hydrogen, methane and minor amounts of C.sub.2 -C.sub.4 hydrocarbons is fed to the methanol synthesis stage together with fresh synthesis gas.

Process of producing gasoline from synthesis gas

A reducing gas containing essentially carbon monoxide and hydrogen and only small amounts of water vapor, carbon dioxide and methane is produced by reacting a normally liquid, volatile hydrocarbon with water vapor in two stages under superatmospheric pressure in the presence of nickel-containing catalysts. The improvement of the invention involves adding from 0.02 to 0.1 standard cubic meter of hydrogen per kilogram hydrocarbon to the hydrocarbons to be gasified, subjecting the resulting mixture to a hydrogenation desulfurization and, after adding up to 1.6 kilogram water vapor per kilogram hydrocarbon, reacting said mixture in a one-part first gasification stage at temperatures of 350.degree.-550.degree. C. in the presence of a catalyst containing from 35-70% by weight nickel on a magnesium-containing support thereby producing a high-methane gas which is reacted further in a second stage at temperatures above 850.degree. C. in contact with an indirectly heated heat resistant nickel catalyst.

Process of producing a reducing gas

Carbon monoxide is produced from light hydrocarbons having an average C number not greater than 15 by catalytic cracking with water vapor in two cracking stages followed by separation of the carbon monoxide from the product gas employing the following steps:

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Friedrichsdorf, Germany

Friedrich W Moller