Soil release agents having allyl-derived sulfonated end caps

Claim 2

A sulfonated oligomeric ester composition comprising the sulfonated product of a preformed, substantially linear ester oligomer, said linear ester oligomer comprising, per mole, (a) 2 moles of terminal units wherein from about I mole to about 2 moles of said terminal units are derived from an olefinically unsaturated component selected from the group consisting of allyl alcohol and methallyl alcohol, and any remaining of said terminal units are other units of said linear ester oligomer; (b) from about 1 mole to about 4 moles of nonionic hydrophile units, said hydrophile units being derived from alkylene oxides, said alkylene oxides comprising from about 50% to 100% ethylene oxide; (c) from about 1.1 moles to about 20 moles of repeat units derived from an aryldicarbonyl component, wherein said aryldicarbonyl component is comprised of from about 50% to 100% dimethylterephthalate, whereby the repeat units derived from said dimethylterephthalate are terephthaloyl; and (d) from about 0.1 moles to about 19 moles of repeat units derived from a diol component selected from the group consisting of C 2 --, C 3 -- and C 4 glycols; wherein the extent of sulfonation of said sulfonated oligomeric ester composition is such that said terminal units are chemically modified by (e) from about 1 mole to about 4 moles of terminal unit substituent groups of formula --SO x M wherein x is 2 or 3, said terminal unit substituent groups being derived from a bisulfite component selected from the group consisting of HSO 3 M wherein M is a conventional water-soluble cation.

Claim 3

A sulfonated oligomeric ester composition according to claim 1 wherein said terminal units of (a) are derived from an olefinically unsaturated component consisting essentially of allyl alcohol; said nonionic hydrophile units of (b) have an average degree of polymerization of from about 4 to about 30 and are derived from an ether component consisting essentially of ethylene oxide; and said repeat units of (c) are derived from a mixture of an aryldicarbonyl component comprised of from about 80% to about 100% dimethylterephthalate; and said diol component of (d) consists essentially of a mixture of ethylene glycol and 1,2-propylene glycol wherein the ethylene glycol: 1,2-propylene glycol mole ratio is in the range from 0:1 to about 0.9:0.1.

Claim 4

A sulfonated oligomeric ester composition according to claim 2 wherein said nonionic hydrophile units (b) have an average degree of polymerization of from about 8 to about 20 and wherein the units (d), the ethylene glycol: 1,2-propylene glycol mole ratio is in the range from 0:1 to about 0.4:0.6.

Claim 5

A sulfonated oligomeric ester composition according to claim 2 which is further characterized in that it comprises the product of a process comprising: in an ester-bond forming procedure, a transesterification step, comprising reacting a mixture of (I) about 2 moles of allyl alcohol ethoxylated to an average degree of polymerization of from about 8 to about 20; and (II) from about 2 to about 7 moles of dimethyl terephthalate; and (III) from about 2 to about 14 moles of 1,2-propylene glycol or mixture thereof with ethylene glycol; wherein the transesterification step is carried out in the presence of a conventional transesterification catalyst; at a transesterification temperature in the range from about 120° C. to about 250° C., at a transesterification pressure in the range from about 0.75 atm. to about 3 atm., for a transesterification time of from about 2 hrs. to about 60 hrs.; followed by an oligomerization step, comprising further reacting said mixture at an oligomerization temperature in the range from about 170° C. to about 250° C., at an oligomerization pressure in the range from about 1×10 -6 atm. to about 0.5 atm., for an oligomerization time of from about 2 hrs. to about 60 hrs.; whereby an allyl end-capped co-oligomeric ester precursor is produced; followed by a radical-initiated olefin sulfonation procedure.

Claim 6

A sulfonated oligomeric ester composition according to claim 4, wherein said radical-initiated olefin sulfonation procedure comprises: at least one step of sulfonating said allyl end-capped co-oligomeric ester precursor, in the presence of water, with a low temperature, free-radical sulfonation initiator and a conventional bisulfite sulfonating reagent; wherein the .reactants are effectively cocontacted in an aqueous reaction mixture and wherein the level of said conventional bisulfite sulfonating agent is from about 1 mole to about 4 moles per mole of said allyl end-capped co-oligomeric ester precursor and wherein the following sulfonation conditions are respected: sulfonation temperature: in the range from about 0° C. to about 100° C.; sulfonation pressure: in the range from about 0.5 atm. to about 3 atm., and sulfonation time period: from about 0.1 hrs. to about 90 hrs.

Claim 7

A sulfonated oligomeric ester composition according to claim 5, wherein said transesterification temperature is in the range from about 160° C. to about 230° C.; said transesterification pressure is in the range from about 1 atm. to about 2 atm.; said transesterification time is in the range from about 5 hrs. to about 25 hrs.; said oligomerization temperature is in the range from about 180° C. to about 220° C.; said oligomerization pressure is in the range from about 1×10 -4 atm. to about 0.05 atm.; and said oligomerization time is in the range from about 5 hrs. to about 25 hrs.

Claim 8

A sulfonated oligomeric ester composition according to claim 6, wherein the low temperature free-radical sulfonation initiator is selected from azo initiators and redox initiators, and wherein the following sulfonation conditions are respected when using the azo initiator: sulfonation temperature: in the range from about 40° C. to about 65° C.; sulfonation pressure: in the range from about 1 atm. to about 3 atm.; and sulfonation time period: from about 10 hrs. to about 30 hrs.; and wherein the following conditions are used with the redox initiator: sulfonation temperature 0° C. to 40° C.; sulfonation pressure 0.5-3 atm; sulfonation time: 0.1-24 hrs.

Claim 9

A sulfonated oligomeric ester composition according to claim 6, wherein the process comprises the additional step of treating the sulfonated product with hydrogen peroxide.

Claim 10

In a process for preparing sulfonated ester compositions useful as functional materials in detergent compositions, said process comprising at least one ester-bond forming procedure and at least one sulfonation procedure, the improvement whereby a particular terminally sulfonated, substantially linear co-oligomeric ester composition is secured without reliance upon a chlorinated compound and without reliance upon a procedure comprising a sulfonation step followed by an ethoxylation step; which improvement comprises the ordered sequence of: (a) in an ester-bond forming procedure, a transesterification step, comprising reacting a mixture of (I) about 2 moles of allyl alcohol ethoxylated to an average degree of polymerization of from about 8 to about 20; together with (II) from about 2 to about 7 moles of dimethyl terephthalate; and (III) from about 2 to about 14 moles of a C 2 -C 4 glycol; in the presence of a conventional transesterification catalyst; at a transesterification temperature in the range from about 120° C. to about 250° C., at a transesterification pressure in the range from about 0.75 atm. to about 3 atm. and for a transesterification time of from about 2 hrs. to about 60 hrs.; followed by an oligomerization step comprising further reacting said mixture at an oligomerization temperature in the range from about 170° C. to about 250° C., at an oligomerization pressure in the range from about 1×10 -6 atm. to about 0.5 atm., and for an oligomerization time of from about 2 hrs. to about 60 hrs.; thereby producing an allyl endcapped co-oligomeric ester precursor; and (b) in a radical-initiated olefin sulfonation procedure, at least one step of sulfonating said allyl end-capped co-oligomeric ester precursor, in the presence of water, with a low temperature, free-radical sulfonation initiator and a conventional bisulfite sulfonating reagent; wherein the reactants are effectively cocontacted in an aqueous reaction mixture and wherein the level of said conventional bisulfite sulfonating agent is from about 1 mole to about 4 moles per mole of said allyl end-capped co-oligomeric ester precursor and wherein the following sulfonation conditions are respected: sulfonation temperature: in the range from about 0° C. to about 100° C.; sulfonation pressure: in the range from about 0.5 atm. to about 3 atm.; and sulfonation time period: from about 0.1 hrs. to about 90 hrs.

Claim 11

In a process for preparing sulfonated ester compositions useful as functional materials in detergent compositions, said process comprising at least one ester-bond forming procedure and at least one sulfonation procedure, the improvement whereby a particular terminally sulfonated, substantially linear co-oligomeric ester composition is secured without reliance upon a chlorinated compound and without reliance upon a procedure comprising a sulfonation step followed by an ethoxylation step; which improvement comprises the ordered sequence of: (a) in an ester-bond forming procedure, a transesterification step, comprising reacting a mixture of (I) about 2 moles of allyl alcohol ethoxylated to an average degree of polymerization of from about 8 to about 20; together with (II) from about 2 to about 7 moles of dimethyl terephthalate; and (III) from about 2 to about 14 moles of a C 2 -C 4 glycol; in the presence of a conventional transesterification catalyst; at a transesterification temperature in the range from about 120° C. to about 250° C., at a transesterification pressure in the range from about 0.75 atm. to about 3 atm. and for a transesterification time of from about 2 hrs. to about 60 hrs.; followed by an oligomerization step comprising further reacting said mixture at an oligomerization temperature in the range from about 170° C. to about 250° C., at an oligomerization pressure in the range from about 1×10 -6 atm. to about 0.5 atm., and for an oligomerization time of from about 2 hrs. to about 60 hrs.; thereby producing an allyl endcapped co-oligomeric ester precursor; and (b) in a radical-initiated olefin sulfonation procedure, at least one step of sulfonating said allyl end-capped co-oligomeric ester precursor, in the presence of water, with a low temperature, free-radical sulfonation initiator and a conventional bisulfite sulfonating reagent; wherein the reactants are effectively cocontacted in an aqueous reaction mixture and wherein the level of said conventional bisulfite sulfonating agent is from about 1 mole to about 4 moles per mole of said allyl end-capped co-oligomeric ester precursor and wherein the following sulfonation conditions are respected: sulfonation temperature: in the range from about 0° C. to about 100° C.; sulfonation pressure: in the range from about 0.5 atm. to about 3 atm.; and sulfonation time period: from about 0.1 hrs. to about 90 hrs.

Claim 12

A sulfonated oligomeric ester composition, in a sodium salt form, consisting essentially of: (i) a substantially linear oligomeric ester backbone, which is comprised of terephthaloyl and oxyalkyleneoxy repeat units, wherein from about 85% to 100% by weight of said backbone is comprised of terephthaloyl and oxy-1,2-propyleneoxy repeat units; and (ii) terminal moieties covalently attached to said backbone, wherein said terminal moieties are derived from compounds selected from the group consisting of allyl alcohol ethoxylate, dimethylterephthalate, and 1,2-propylene diol, provided that from about 70% to 100% of said terminal moieties are selected from the group consisting of: --(E n )--(CH 2 --CH{SO 3 N a }--CH 2 {SO 3 Na}), --(E n )--(CH 2 --CH{SO 2 Na}--CH 2 {SO 3 Na}), and --(E n )--(CH 2 --CH 2 --CH 2 {SO 3 Na}); wherein (E n ) is poly(oxyethylene)oxy and n is in the range from about 8 to about 20; and wherein said composition comprises from about 5% to about 40%, by weight, of end-cap moieties --(CH 2 --CH{SO 3 Na}--CH 2 {SO 3 Na}), --(CH 2 --CH{SO 2 N a })--CH 2 (SO 3 Na}) and --(CH 2 --CH 2 --CH 2 (SO 3 N a }).

Claim 13

A sulfonated oligomeric ester composition, in a sodium salt form, consisting essentially of: (i) a substantially linear oligomeric ester backbone, which is comprised of terephthaloyl and oxyalkyleneoxy repeat units, wherein from about 85% to 100% by weight of said backbone is comprised of terephthaloyl and oxy-1,2-propyleneoxy repeat units; and (ii) terminal moieties covalently attached to said backbone, wherein said terminal moieties are derived from compounds selected from the group consisting of allyl alcohol ethoxylate, dimethylterephthalate, and 1,2-propylene diol, provided that from about 70% to 100% of said terminal moieties are selected from the group consisting of: --(E n )--(CH 2 --CH{SO 3 N a }--CH 2 {SO 3 Na}), --(E n )--(CH 2 --CH{SO 2 Na}--CH 2 {SO 3 Na}), and --(E n )--(CH 2 --CH 2 --CH 2 {SO 3 Na}); wherein (E n ) is poly(oxyethylene)oxy and n is in the range from about 8 to about 20; and wherein said composition comprises from about 5% to about 40%, by weight, of end-cap moieties --(CH 2 --CH{SO 3 Na}--CH 2 {SO 3 Na}), --(CH 2 --CH{SO 2 N a })--CH 2 (SO 3 Na}) and --(CH 2 --CH 2 --CH 2 (SO 3 N a }).

Claim 14

The sodium salt form of a sulfonated oligomeric ester according to claim 10, wherein the percentage by weight of the end-cap moieties --(CH 2 --CH{SO 3 Na}--CH 2 {SO 3 Na}), --(CH 2 --CH{SO 2 Na}--CH 2 {SO 3 Na}) and --(CH 2 --CH 2 --CH 2 {SO 3 Na}) is in the range from about 10% to about 30%.

Claim 15

The sodium salt form of a sulfonated oligomeric ester according to claim 10, wherein the mole ratio of the doubly sulfonated end-cap moieties: --(CH 2 --CH{SO 3 Na}--CH 2 {SO 3 Na}) and --(CH 2 --CH{SO 2 Na})--CH 2 {SO 3 Na}) in relation to the singly sulfonated end-cap moieties: --(CH 2 --CH 2 --CH 2 {SO 3 Na}), is in the range from 1:5 to about 1:0.

Claim 16

The sodium salt form of a sulfonated oligomeric ester according to claim 10, wherein the mole ratio of the doubly sulfonated end-cap moieties: --(CH 2 --CH{SO 3 Na}--CH 2 {SO 3 Na}) and --(CH 2 --CH{SO 2 Na}--CH 2 {SO 3 Na}), in relation to the singly sulfonated end-cap moieties: --(CH 2 --CH 2 --CH 2 {SO 3 Na}), is in the range from about 2:1 to about 1:0.

Claim 17

A detergent composition, comprising at least about 0.05% by weight of the composition of claim 1.

Claim 18

A built laundry detergent according to claim 14, comprising from about 5% to about 50% by weight of detersive surfactant and from about 5% to about 60% by weight of detergency builder.

Claim 19

A composition according to claim 15 wherein the builder is a member selected from the group consisting of polycarboxylate builders, zeolite builders, phosphate builders, and mixtures thereof.

Claim 20

A composition according to claim 16 wherein the builder is selected from oxodisuccinate salts, tartrate monosuccinate salts, tartrate disuccinate salts, and mixtures thereof.