Preparation of acyloxy benzene sulfonate

Claim 2

A process for making an acyloxy benzene sulfonate salt of at least about 80 weight percent purity on a total composition dry weight basis from a corresponding acyloxy benzene comprising the steps of (a) contacting substantially pure acyloxy benzene with SO 3 at a temperature ranging from about -20° to 50° C. to produce an intermediate reaction product which comprises about a 1:1 molar adduct of said SO 3 and said acyloxy benzene, (b) maintaining said intermediate reaction product at an average temperature in the range from about 25° to 75° C. for a time inversely ranging from about 0.1 to 4 hours sufficient to produce a product composition containing at least about 80 weight percent of the corresponding acyloxy benzene sulfonic acid, and (c) admixing the resulting said acyloxy benzene sulfonic acid with an aqueous solution of a base of a cation selected from the group consisting of alkali metal salts, alkaline earth metals, and ammonium to produce an aqueous solution containing the corresponding salt of said acyloxy benzene sulfonic acid.

Claim 3

The process of claim 1 wherein said acyloxy benzene is cahracterized by the formula: ##STR3## where R is a saturated aliphatic group containing from 2 through 19 carbon atoms.

Claim 4

The process of claim 2 wherein said sulfonation is carried out in a zone wherein the average temperature ranges from about -30° to +50° C., and the mole ratio of said SO 3 to said acyloxy benzene ranges from about 0.9:1 to 1.1:1.

Claim 5

The process of claim 2 wherein each said aliphatic group is an alkyl group which contains from 7 through 11 carbon atoms.

Claim 6

The process of claim 2 wherein said contacting is carried out in a liquid phase in the presence of a diluent.

Claim 7

The process of claim 5 wherein said contacting is carried out with said acyloxybenzene being in a liquid state.

Claim 8

The process of claim 1 wherein said digesting is carried out at an average temperature ranging from about 40° to 75° C.

Claim 9

The process of claim 1 wherein said admixing is carried out continuously and the product neutralized solution has a pH in the range from about 4.5 to 7.

Claim 10

The process of claim 1 wherein the final product solution has a pH ranging from about 3 to 8 and wherein the concentration of said salt of said acyloxy benzene sulfonic acid ranges from about 5 to 60 weight percent based on total aqueous solution weight.

Claim 11

A process for making an acyloxy benzene sulfonate salt which has an APHA color that is less that about 100 comprising the steps of sequentially: (A) contacting SO 3 with at least one acyloxybenzene of the formula: ##EQU1## where R is a saturated aliphatic group containing from about 2 to 19 carbon atoms inclusive under liquid phase conditions in the presence of a substantially inert liquid to produce a reaction product wherein the combined mole ratio of SO 3 to acyloxybenzene ranges from about 0.9 to 1.1, (B) evaporating said inert liquid from said reaction product at a rate sufficient to maintain said reaction product at a temperature from about -10° to 15° C. (C) maintaining said resulting reaction product at a temperature in the range from about 10° to 75° C. for a time inversely ranging from about 0.1 to about 4 hours until said reaction product has been substantially completely rearranged, thereby to produce acyloxybenzene sulfonic acid, and (D) admixing said acid with dilute aqueous base solution under liquid phase conditions at a temperature below about 35° C.

Claim 12

A process for making an acyloxy benzene sulfonate salt which has an APHA color that is less that about 100 comprising the steps of sequentially: (A) contacting SO 3 with at least one acyloxybenzene of the formula: ##EQU1## where R is a saturated aliphatic group containing from about 2 to 19 carbon atoms inclusive under liquid phase conditions in the presence of a substantially inert liquid to produce a reaction product wherein the combined mole ratio of SO 3 to acyloxybenzene ranges from about 0.9 to 1.1, (B) evaporating said inert liquid from said reaction product at a rate sufficient to maintain said reaction product at a temperature from about -10° to 15° C. (C) maintaining said resulting reaction product at a temperature in the range from about 10° to 75° C. for a time inversely ranging from about 0.1 to about 4 hours until said reaction product has been substantially completely rearranged, thereby to produce acyloxybenzene sulfonic acid, and (D) admixing said acid with dilute aqueous base solution under liquid phase conditions at a temperature below about 35° C.

Claim 13

The process of claim 10 wherein said acyloxybenzene sulfonic acid is dissolved in water under liquid phase conditions at a temperature below about 5° C. to produce a dilute aqueous acid solution and said solution is then so admixed with said base solution.

Claim 14

The process of claim 10 wherein said resulting mixed slurry is spray dried.

Claim 15

In a sulfonation process for making a sulfonated salt by sulfonating with SO 3 and neutralizing, the improvement which comprises reacting an acyloxy benzene with SO 3 at low temperatures followed by a controlled rearrangement step between said sulfonating and said neutrualizing, said controlled rearrangement step comprising maintaining the sulfonation reaction product at a temperature of from about 15° to 75° C. until said reaction product is substantially completely rearranged.

Claim 16

In a sulfonation process for making a sulfonated salt by sulfonating with SO 3 and neutralizing, the improvement which comprises reacting an acyloxy benzene with SO 3 at low temperatures followed by a controlled rearrangement step between said sulfonating and said neutrualizing, said controlled rearrangement step comprising maintaining the sulfonation reaction product at a temperature of from about 15° to 75° C. until said reaction product is substantially completely rearranged.