Alkoxylation process

Claim 2

A process for the preparation of alkanol alkoxylates which comprises reacting in an alkoxylation reaction mixture an alkanol reactant comprising one or more alkanols having carbon numbers in the range from about 6 to 30, inclusive, with an alkylene oxide reactant comprising one or more alkylene oxides having carbon numbers in the range from 2 to 4, inclusive, in the presence of a catalytically-effective amount of a co-catalyst combination comprising as a first component one or more soluble basic compounds of magnesium and as a second component one or more soluble compounds of at least one element selected from the group consisting of aluminum, boron, zinc, titanium, silicon, molybdenum, vanadium, gallium, germanium, yttrium, zirconium, niobium, cadmium, indium, tin, antimony, tungsten, hafnium, tantalum, thallium, lead, and bismuth, said co-catalyst combination comprising at least about 5 percent by mol of said second component, calculated on mols of said first component.

Claim 3

The process of claim 1, wherein the second component of the co-catalyst combination is one or more soluble compounds of at least one element selected from the group consisting of aluminum, boron, zinc, and titanium.

Claim 4

The process of claim 2, wherein the second component of the co-catalyst combination is one or more soluble compounds of at least one element selected from the group consisting of aluminum and boron.

Claim 5

The process of claim 3, wherein the second component of the co-catalyst combination is one or more soluble compounds of aluminum.

Claim 6

The process of claim 1, claim 2, claim 3, or claim 4, wherein the co-catalyst combination comprises between about 10 and 100 percent by mol of said second component, calculated on mols of said first component.

Claim 7

The process of claim 1, claim 2, claim 3, or claim 4, wherein the co-catalyst combination comprises between about 15 and 50 percent by mol of said second component, calculated on mols of said first component.

Claim 8

The process of claim 1, wherein the first component and the second component are each individually selected from the group consisting of alcoholates, ammoniates, amides, thiolates, thiophenoxides, nitrides, thiocyanates, and carboxylates, and substances to which such compounds are converted in situ in the alkoxylation reaction mixture.

Claim 9

The process of claim 2, wherein the first component and the second component are each individually selected from the group consisting of alcoholates, ammoniates, amides, thiolates, thiophenoxides, nitrides, thiocyanates, and carboxylates, and substances to which such compounds are converted in situ in the alkoxylation reaction mixture.

Claim 10

The process of claim 3, wherein the first component and the second component are each individually selected from the group consisting of alcoholates, ammoniates, amides, thiolates, thiophenoxides, nitrides, thiocyanates, and carboxylates, and substances to which such compounds are converted in situ in the alkoxylation reaction mixture.

Claim 11

The process of claim 2, wherein the first component and the second component are each individually selected from the group consisting of alkoxides having a carbon number in the range from 1 to about 30.

Claim 12

The process of claim 3, wherein the first component and the second component are each individually selected from the group consisting of alkoxides having a carbon number in the range from 1 to about 30.

Claim 13

The process of claim 4, wherein the first component and the second component are each individually selected from the group consisting of alkoxides having carbon number in the range from 1 to about 6.

Claim 14

The process of claim 4, wherein the first component is one or more soluble basic compounds selected from the group consisting of magnesium methoxide, magnesium ethoxide and magnesium isopropoxide, and wherein the second component is one or more soluble compounds selected from the group consisting of aluminum ethoxide and aluminum isopropoxide.

Claim 15

The process of claim 7, claim 8, claim 9, claim 10, claim 11, claim 12, or claim 13, wherein the co-catalyst combination comprises between about 10 and 100 percent by mol of said second component, calculated on mols of said first component.

Claim 16

The process of claim 7, claim 8, claim 9, claim 10, claim 11, claim 12, or claim 13, wherein the co-catalyst combination comprises between about 15 and 50 percent by mol of said second component, calculated on mols of said first component.

Claim 17

The process of claim 5, wherein the co-catalyst combination comprises between about 0.5 and 15 percent by mole of the first component, calculated on the moles of the alkanol reactant.

Claim 18

The process of claim 6, wherein the co-catalyst combination comprises between about 0.5 and 15 percent by mole of the first component, calculated on moles of the alkanol reactant, wherein the alkanol reactant has a carbon number in the range from about 8 to 18, inclusive, and wherein the alkylene oxide is ethylene oxide.

Claim 19

The process of claim 14, wherein the co-catalyst combination comprises between about 0.5 and 15 percent by mole of the first component, calculated on moles of the alkanol reactant, wherein the alkanol reactant has a carbon number in the range from about 8 to 18, inclusive, and wherein the alkylene oxide is ethylene oxide.

Claim 20

The process of claim 15, wherein the co-catalyst combination comprises between about 0.5 and 15 percent by mole of the first component, calculated on moles of the alkanol reactant, wherein the alkanol reactant has a carbon number in the range from about 8 to 18, inclusive, and wherein the alkylene oxide is ethylene oxide.

Claim 21

A process for the preparation of alkanol ethoxylates which comprises reacting in an ethoxylation reaction mixture of basic pH at a temperature in the range from about 150° to 190° C. an alkanol reactant comprising one or more alkanols having carbon numbers in the range from about 10 to 16, inclusive, with ethylene oxide in the presence of a co-catalyst combination comprising as a first component between about 0.5 and 15 percent by mole, calculated on alkanol reactant, of one or more soluble basic compounds selected from the group consisting of magnesium methoxide, magnesium ethoxide, magnesium isopropoxide, and the substances to which magnesium ethoxide and magnesium isopropoxide are converted in situ in the reaction mixture and as a second component at least about 15 percent by mol, calculated on mols of first component, of one or more soluble compounds selected from the group consisting of aluminum ethoxide, aluminum isopropoxide and the substances to which aluminum ethoxide and aluminum isopropoxide are converted in situ in the reaction mixture.

Claim 22

A process for the preparation of alkanol ethoxylates which comprises reacting in an ethoxylation reaction mixture of basic pH at a temperature in the range from about 150° to 190° C. an alkanol reactant comprising one or more alkanols having carbon numbers in the range from about 10 to 16, inclusive, with ethylene oxide in the presence of a co-catalyst combination comprising as a first component between about 0.5 and 15 percent by mole, calculated on alkanol reactant, of one or more soluble basic compounds selected from the group consisting of magnesium methoxide, magnesium ethoxide, magnesium isopropoxide, and the substances to which magnesium ethoxide and magnesium isopropoxide are converted in situ in the reaction mixture and as a second component at least about 15 percent by mol, calculated on mols of first component, of one or more soluble compounds selected from the group consisting of aluminum ethoxide, aluminum isopropoxide and the substances to which aluminum ethoxide and aluminum isopropoxide are converted in situ in the reaction mixture.

Claim 23

A process for the preparation of alkanol ethoxylates which comprises reacting in a basic ethoxylation reaction mixture at a temperature in the range from about 150° to 190° C. an alkanol reactant comprising one or more alkanols having carbon numbers in the range from about 10 to 16 inclusive, with ethylene oxide in the presence of a co-catalyst combination comprising as a first component between about 0.5 and 15 percent by mole, calculated on alkanol reactant, of one or more magnesium alkoxides having from 1 to about 30 carbon atoms and as a second component between about 10 and 100% m, calculated on moles of first component, of one or more aluminum alkoxides having from 1 to about 30 carbon atoms.

Claim 24

A process for the preparation of alkanol ethoxylates which comprises reacting in a basic ethoxylation reaction mixture at a temperature in the range from about 150° to 190° C. an alkanol reactant comprising one or more alkanols having carbon numbers in the range from about 10 to 16 inclusive, with ethylene oxide in the presence of a co-catalyst combination comprising as a first component between about 0.5 and 15 percent by mole, calculated on alkanol reactant, of one or more magnesium alkoxides having from 1 to about 30 carbon atoms and as a second component between about 10 and 100% m, calculated on moles of first component, of one or more aluminum alkoxides having from 1 to about 30 carbon atoms.