Reaction of methanol with synthesis gas

Claim 2

In a process for reacting methanol in the liquid phase at elevated temperature and superatmospheric pressure with a gas comprising carbon monoxide and hydrogen to form a product comprising methyl acetate, acetaldehyde, and dimethylacetal, the improvement which comprises utilizing a catalytic amount of a halide-free catalyst consisting essentially of a cobalt carbonyl in complex combination with an organic nitrogen ligand of from one to 25 carbon atoms having no ethylenic or acetylenic unsaturation and no elements other than carbon, nitrogen, oxygen, and hydrogen, said ligand containing in its molecule from 1 to 5 Lewis base nitrogen atoms which are present as urea, tertiary amino or nitrilo nitrogen atoms, said ligand being, when said nitrogen atoms are urea nitrogens, a urea of the formula ##STR2## wherein R is hydrogen or a C 1 to C 9 hydrocarbon group and wherein each R group may be alike or different.

Claim 3

In a process for reacting methanol in the liquid phase at elevated temperature and superatmospheric pressure with a gas comprising carbon monoxide and hydrogen to form a product comprising methyl acetate, acetaldehyde, and dimethylacetal, the improvement which comprises utilizing a catalytic amount of a halide-free catalyst consisting essentially of a cobalt carbonyl in complex combination with an organic nitrogen ligand of from one to 25 carbon atoms having no ethylenic or acetylenic unsaturation and no elements other than carbon, nitrogen, oxygen, and hydrogen and which is a member of the group consisting of glutaronitrile, ortho-phenylenediacetonitrile, 2-hydroxypyridine, tetramethylethylenediamine, 2-cyanophenol, and urea.

Claim 4

In a process for reacting methanol in the liquid phase at elevated temperature and superatmospheric pressure with a gas comprising carbon monoxide and hydrogen to form a product comprising methyl acetate, acetaldehyde, and dimethylacetal, the improvement which comprises utilizing a catalytic amount of a halide-free catalyst consisting essentially of a cobalt carbonyl in complex combination with an organic nitrogen ligand of from one to 25 carbon atoms having no ethylenic or acetylenic unsaturation and no elements other than carbon, nitrogen, oxygen, and hydrogen and which is a member of the group consisting of glutaronitrile, ortho-phenylenediacetonitrile, 2-hydroxypyridine, tetramethylethylenediamine, 2-cyanophenol, and urea.

Claim 5

In a process for reacting methanol in the liquid phase at elevated temperature and superatmospheric pressure with a gas comprising carbon monoxide and hydrogen to form a product comprising methyl acetate, acetaldehyde, and dimethylacetal, the improvement which comprises utilizing a catalytic amount of a halide-free catalyst consisting essentially of a cobalt carbonyl in complex combination with an organic nitrogen ligand of from one to 25 carbon atoms having no ethylenic or acetylenic unsaturation and no elements other than carbon, nitrogen, oxygen, and hydrogen and which is a member of the group consisting of dinitriles having from 3 to 18 carbon atoms and ureas of the formula R 2 NCONR 2 wherein R is hydrogen or a C 1 to C 9 hydrocarbon group and wherein the R groups may be alike or different.

Claim 6

In a process for reacting methanol in the liquid phase at elevated temperature and superatmospheric pressure with a gas comprising carbon monoxide and hydrogen to form a product comprising methyl acetate, acetaldehyde, and dimethylacetal, the improvement which comprises utilizing a catalytic amount of a halide-free catalyst consisting essentially of a cobalt carbonyl in complex combination with an organic nitrogen ligand of from one to 25 carbon atoms having no ethylenic or acetylenic unsaturation and no elements other than carbon, nitrogen, oxygen, and hydrogen and which is a member of the group consisting of dinitriles having from 3 to 18 carbon atoms and ureas of the formula R 2 NCONR 2 wherein R is hydrogen or a C 1 to C 9 hydrocarbon group and wherein the R groups may be alike or different.

Claim 7

The improvement of claim 3 wherein an amount of said catalyst is used which will provide from about 2 to 50 millimoles of cobalt carbonyl, calculated as dicobalt octacarbonyl, per mole of methanol; the amount of said nitrogen ligand is such as to provide an atomic ration of nitrogen atoms to cobalt atoms of from about 0.5:1 to 2.0:1; the process is conducted at about 175° to 215° C. and about 130 to 400 atomspheres absolute; and said gas comprises about 30 to 60 mole percent carbon monoxide and 40 to 70 mole percent hydrogen.

Claim 8

In a process for reacting methanol in the liquid phase at elevated temperature and superatmospheric pressure with a gas comprising carbon monoxide and hydrogen to form a product comprising methyl acetate, acetaldehyde, and dimethylacetal, the improvement which comprises utilizing a catalytic amount of a halide-free catalyst consisting essentially of a cobalt carbonyl in complex combination with a urea of the formula R 2 NCONR 2 wherein R is hydrogen or a C 1 to C 9 hydrocarbon group and wherein the R groups may be alike or different, the amount of said catalyst used being such as to provide from about 2 to 50 millimoles of cobalt carbonyl, calculated as dicobalt octacarbonyl, per mole of methanol and the amount of said urea being such as to provide an atomic ratio of nitrogen atoms to cobalt atoms of from about 0.5:1 to 2.0:1, said process being conducted at about 175° to 215° C. and about 130 to 400 atmospheres absolute and said gas comprising about 30 to 60 mole percent carbon monoxide and 40 to 70 mole percent hydrogen.

Claim 9

In a process for reacting methanol in the liquid phase at elevated temperature and superatmospheric pressure with a gas comprising carbon monoxide and hydrogen to form a product comprising methyl acetate, acetaldehyde, and dimethylacetal, the improvement which comprises utilizing a catalytic amount of a halide-free catalyst consisting essentially of a cobalt carbonyl in complex combination with a urea of the formula R 2 NCONR 2 wherein R is hydrogen or a C 1 to C 9 hydrocarbon group and wherein the R groups may be alike or different, the amount of said catalyst used being such as to provide from about 2 to 50 millimoles of cobalt carbonyl, calculated as dicobalt octacarbonyl, per mole of methanol and the amount of said urea being such as to provide an atomic ratio of nitrogen atoms to cobalt atoms of from about 0.5:1 to 2.0:1, said process being conducted at about 175° to 215° C. and about 130 to 400 atmospheres absolute and said gas comprising about 30 to 60 mole percent carbon monoxide and 40 to 70 mole percent hydrogen.

Claim 10

The improvement of claim 5 wherein said urea is H 2 NCONH 2 .