Hydrocarbon synthesis using a rare earth promoted metal silicate

Claim 2

A process which comprises contacting a charge stock comprising hydrogen and at least one carbon oxide selected from the group consisting of CO and CO 2 wherein the molar ratio of hydrogen to combined carbon oxide is from 1:1 to 4:1 under reaction conditions including a temperature of from 300° F. to 500° F. with a catalyst consisting essentially of a rare earth promoted metal silicate characterized as having repeating units of the structural formula: [(1=x)Ni.sup.a + xRu.sup.b ].sub.n (OH).sub.4 Si.sub.2 O.sub.5.wH.sub.2 O where x is a number from 0 to 1, this number expressing the atomic fraction of the metals nickel and ruthenium; a is the valence of nickel; b is the valence of ruthenium; n is a number equal in value to that defined by the ratio 6/[a(1=x) + bx] and w is a number ranging from 0 to 4; and thereafter recovering a product, which product, on a methane-free hydrocarbon basis contains at least 60 mole percent of low molecular weight hydrocarbons having from 2 to 6 carbon atoms per molecule.

Claim 3

A process according to claim 1 wherein the metal silicate is nickel chrysotile.

Claim 4

A process according to claim 2 wherein the amount of rare earth metal is from 0.5 to 25 weight percent of the final catalyst.

Claim 5

A process according to claim 3 wherein the rare earth metal is thorium.

Claim 6

A process according to claim 3 wherein the rare earth metal is lanthanum.

Claim 7

A process according to claim 3 wherein the rare earth metal is cerium.

Claim 8

A process according to claim 3 wherein the rare earth metal is praesodymium.

Claim 9

A process according to claim 3 wherein the rare earth metal is a mixture of rare earth metals.

Claim 10

A process according to claim 8 wherein the mixture of rare earth metals is thorium and lanthanum.

Claim 11

A process according to claim 8 wherein the mixture of rare earth metals is thorium and praesodymium.

Claim 12

A process according to claim 3 wherein the rare earth metal is added to the nickel chrysotile by deposition.

Claim 13

A process according to claim 11 wherein the rare earth metal is deposited from an aqueous solution of a rare earth metal nitrate.

Claim 14

A process according to claim 12 wherein the rare earth metal nitrate is thorium nitrate.

Claim 15

A process according to claim 12 wherein the rare earth metal nitrate is praesodymium nitrate.

Claim 16

A process according to claim 3 wherein the rare earth metal is incorporated into the catalyst during the preparation of the nickel chrysotile.

Claim 17

A process according to claim 15 wherein the nickel chrysotile is a synthetic nickel chrysotile prepared by combining a hydrous silicate solution with a metal oxide or hydroxide solution containing a rare earth salt in an alkaline medium at a pH above 10; and thereafter calcining.

Claim 18

A process according to claim 16 wherein the rare earth salt is thorium nitrate.

Claim 19

A process according to claim 16 wherein the rare earth salt is lanthanum nitrate.

Claim 20

A process according to claim 16 wherein the rare earth salt is cerium nitrate.

Claim 21

A process according to claim 16 wherein the rare earth salt is praesodymium nitrate.

Claim 22

A process according to claim 16 wherein the rare earth metal salt is a mixture of rare earth metal salts.

Claim 23

A process according to claim 21 wherein the rare earth metal salt mixture is comprised of thorium nitrate and lanthanum nitrate.

Claim 24

A process according to claim 21 wherein the rare earth metal salt mixture is comprised of thorium nitrate and praesodymium nitrate.

Claim 25

A process according to claim 16 wherein the pH is 12 to 14.

Claim 26

A process according to claim 2 wherein the methane-free hydrocarbon product contains at least 70 mole percent of paraffins having 2 to 6 carbon atoms per molecule.

Claim 27

A process according to claim 2 wherein the methane-free hydrocarbon product contains at least 90 mole percent of paraffins having from 2 to 6 carbon atoms per molecule.

Claim 28

A process which comprises contacting a charge stock comprising hydrogen and at least one carbon oxide selected from the group consisting of CO and CO 2 wherein the molar ratio of hydrogen to combined carbon oxide is from 1.5:1 to 2.5:1 under reaction conditions including a temperature of from 350° F. to 450° F. with a catalyst consisting essentially of a rare earth metal promoted metal silicate characterized as having repeating units of the structural formula: [(1-x)Ni.sup.a + xRu.sup.b ].sub.n (OH).sub.4 SiO.sub.2 O.sub.5.wH.sub.2 O where x is a number from 0 to 1, this number expressing the atomic fraction of the metals nickel and ruthenium; a is the valence of nickel; b is the valence of ruthenium; n is a number equal in value to that defined by the ratio 6/[a(1-x) + bx] and w is a number ranging from 0 to 4; and thereafter recovering a hydrocarbon product consisting of at least about 50 weight percent on a methane free basis of paraffins having at least two carbon atoms per molecule and where in said hydrocarbon product the hydrocarbon distribution is such that at least 60 mole percent of said hydrocarbon product has from 2 to 6 carbon atoms per molecule.

Claim 29

A process which comprises contacting a charge stock comprising hydrogen and at least one carbon oxide selected from the group consisting of CO and CO 2 wherein the molar ratio of hydrogen to combined carbon oxide is from 1.5:1 to 2.5:1 under reaction conditions including a temperature of from 350° F. to 450° F. with a catalyst consisting essentially of a rare earth metal promoted metal silicate characterized as having repeating units of the structural formula: [(1-x)Ni.sup.a + xRu.sup.b ].sub.n (OH).sub.4 SiO.sub.2 O.sub.5.wH.sub.2 O where x is a number from 0 to 1, this number expressing the atomic fraction of the metals nickel and ruthenium; a is the valence of nickel; b is the valence of ruthenium; n is a number equal in value to that defined by the ratio 6/[a(1-x) + bx] and w is a number ranging from 0 to 4; and thereafter recovering a hydrocarbon product consisting of at least about 50 weight percent on a methane free basis of paraffins having at least two carbon atoms per molecule and where in said hydrocarbon product the hydrocarbon distribution is such that at least 60 mole percent of said hydrocarbon product has from 2 to 6 carbon atoms per molecule.

Claim 30

A process according to claim 27 wherein the rare earth metal is thorium and the amount of rare earth metal is from 0.5 to 10 weight percent of the final catalyst.

Claim 31

A process according to claim 27 wherein said rare earth metal is a mixture of rare earth metals and the amount of said rare earth metals is from 0.5 to 10 weight percent of the final catalyst.

Claim 32

A process according to claim 27 wherein the metal silicate is nickel chrysotile; the hydrogen to combined carbon oxide ratio is from 1.5:1 to about 2:1; the reaction temperature is from 375° F. to 425° F.

Claim 33

A process according to claim 30 wherein the rare earth metal is thorium and the amount of rare earth metal is from 0.5 to 10. weight percent of the final catalyst.

Claim 34

A process according to claim 30 wherein said rare earth metal is a mixture of rare earth metals and the amount of said rare earth metals is from 0.5 to 10 weight percent of the final catalyst.

Claim 35

A process according to claim 27 wherein the hydrocarbon distribution in said hydrocarbon product is such that more than 50% of said product has from 3 to 5 carbon atoms per molecule.