Process for preparing nonionic surfactants-oxyalkylation with calcium and/or strontium catalysts
AssigneeUnion Carbide Corporation
InventorsJames H. McCain, Louis F. Theiling, Jr.
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AssigneeUnion Carbide Corporation
InventorsJames H. McCain, Louis F. Theiling, Jr.
Estimating the term…
The process for preparing nonionic surfactants wherein a narrower molecular weight distribution is obtained by the use of a calcium and/or strontium catalyst which comprises reacting a reactive hydrogen compound selected from the group consisting of monohydric alcohols having from about 8 to about 20 carbon atoms and a difunctional polypropylene oxide polymer having an average molecular weight in the range of 1000 to 5000 with an alkylene oxide having 2 to 4 carbon atoms at a temperature at which the reaction proceeds in the presence of at least a catalytic amount of a basic salt of calcium and/or strontium selected from the group consisting of hydroxide, alkoxide and phenoxides and a catalytic amount of an oxyalkylation catalyst promoter.
The method for the alkoxylation of a reactive hydrogen compound selected from the group consisting of monohydric alcohols having between about 8 and about 25 carbon atoms, both branched and linear, and a difunctional polypropylene oxide polymer having an average molecular weight in the range of 1000 to 5000 comprising contacting said reactive hydrogen compound with an alkylene oxide having between 2 and 4 carbon atoms in the presence of a catalyst selected from the group consisting of calcium alkoxides, strontium alkoxides, calcium phenoxides and strontium phenoxides and an oxyalkylation catalyst promoter selected from the group consisting of superphosphoric acid, phosphoric acid, sulfuric acid, alkali metal and alkaline earth metal dihydrogen phosphates and dihydrogen diphosphates, alkyl, aryl, araalkyl and alkyaryl dihydrogen phosphates, monoalkyl hydrogen sulfates, carbon dioxide, carbonic acid, alkali metal bicarbonates, oxides of phosphorus, sulfur trioxide, sulfur dioxide and sulfurous acid at a temperature between about 50.degree. C. and about 400.degree. C. employing about 2 to about 50 moles of alkylene oxide per mole of reactive hydrogen.
Dependencies are inferred from the claim text.