Renewable plasticizer alcohols from olefin oligomers and methods for making the same
US-9938214-B1 · Apr 10, 2018 · US
US10836697B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10836697-B2 |
| Application number | US-201816218945-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 13, 2018 |
| Priority date | Jun 28, 2013 |
| Publication date | Nov 17, 2020 |
| Grant date | Nov 17, 2020 |
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Processes to prepare lightly branched surfactant products comprise combining at least one olefin and a coordination-insertion catalyst under conditions such that at least one oligomer product is formed. The surfactant products comprise a main carbon chain containing an average of between 0.5 and 2.5 branches, wherein more than 50% of the branches are ethyl branches, wherein the branches are located more than one carbon away from each end of the main carbon chain in more than 20% of surfactant product molecules.
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What is claimed is: 1. A process for preparing an alcohol product comprising: (1) combining at least one olefin and at least one coordination-insertion catalyst and, optionally, an alpha-olefin, wherein the coordination-insertion catalyst is selected from the group consisting of and combinations thereof, and has an ethylene/octene reactivity ratio up to 20 at an operating reactor temperature, and a kinetic chain length up to 20 monomer units; under conditions such that at least one oligomer product is formed, wherein the oligomer product includes a main carbon chain containing an average of between 0.5 and 2.5 branches, wherein more than 50% of the branches are ethyl branches, wherein the branches are located on average more than one carbon away from each end of the main carbon chain in more than 20% of oligomer product molecules, wherein the branches are situated at a second carbon relative to an unsaturated end of the main carbon chain in less than 40% of the oligomer product molecules, and wherein the oligomer product contains greater than 50% vinyl olefin; (2) fractionating the oligomer product to produce a fractionated oligomer product, such that the average carbon number of the fractionated oligomer product is between 8 and 28; (3) hydroformylating the fractionated oligomer product to produce an aldehyde product; and (4) hydrogenating the aldehyde product to produce the alcohol product. 2. A process according to claim 1 , further comprising alkoxylating the alcohol product to produce an alkoxylate surfactant product. 3. A process according to claim 2 , further comprising sulfating the alkoxylate surfactant product to produce an anionic ether sulfate surfactant product. 4. A process according to claim 1 , further comprising sulfating the alcohol product to produce an anionic sulfate surfactant product. 5. A process according to claim 1 , wherein the at least one olefin is ethylene and an alpha-olefin is not used. 6. A process according to claim 1 , wherein the at least one olefin is an olefin mixture. 7. A process according to claim 6 , wherein the olefin mixture includes olefins with vinyl groups, olefins with vinylidene groups, and olefins with vinylene groups. 8. A process according to claim 1 , further comprising use of a rhodium catalyst with an organophosphorus ligand in the hydroformylating step (3). 9. A process for preparing an alcohol product comprising: (1) combining at least one olefin and at least one coordination-insertion catalyst and, optionally, an alpha-olefin, wherein the coordination-insertion catalyst is a metal-ligand complex of formula wherein M is the metal center, and is a Group 4 metal selected from titanium, zirconium or hafnium; T is an optional bridging group which, if present is selected from dialkylsilyl, diarylsilyl, dialkylmethyl, ethylenyl (—CH 2 —CH 2 —) or hydrocarbylethylenyl wherein one, two, three or four of the hydrogen atoms in ethylenyl are substituted by hydrocarbyl, where hydrocarbyl can be independently C 1 to C 16 alkyl or phenyl, tolyl, or xylyl, and when T is present, the catalyst represented can be in a racemic or a meso form; L 1 and L 2 are the same or different cyclopentadienyl, indenyl, tetrahydroindenyl or fluorenyl rings, optionally substituted, that are each bonded to M, or L 1 and L 2 are the same or different cyclopentadienyl, indenyl, tetrahydroindenyl or fluorenyl, which are optionally substituted; Z is nitrogen, oxygen or phosphorus; R′ is a cyclic linear or branched C 1 to C 40 alkyl or substituted alkyl group; and X 1 and X 2 are, independently, hydrogen, halogen, hydride radicals, hydrocarbyl radicals, substituted hydrocarbyl radicals, halocarbyl radicals, substituted halocarbyl radicals, silylcarbyl radicals, substituted silylcarbyl radicals, germylcarbyl radicals, or substituted germylcarbyl radicals; or both X are joined and bound to the metal atom to form a metallacycle ring containing from 3 to 20 carbon atoms; or both together can be an olefin, diolefin or aryne ligand, and has an ethylene/octene reactivity ratio up to 20 at an operating reactor temperature, and a kinetic chain length up to 20 monomer units; under conditions such that at least one oligomer product is formed, wherein the oligomer product includes a main carbon chain containing an average of between 0.5 and 2.5 branches, wherein more than 50% of the branches are ethyl branches, wherein the branches are located on average more than one carbon away from each end of the main carbon chain in more than 20% of oligomer product molecules, wherein the branches are situated at a second carbon relative to an unsaturated end of the main carbon chain in less than 40% of the oligomer product molecules, and wherein the oligomer product contains greater than 50% vinyl olefin; (2) fractionating the oligomer product to produce a fractionated oligomer product, such that the average carbon number of the fractionated oligomer product is between 8 and 28; (3) hydroformylating the fractionated oligomer product to produce an aldehyde product; and (4) hydrogenating the aldehyde product to produce the alcohol product. 10. A process according to claim 9 , further comprising alkoxylating the alcohol product to produce an alkoxylate surfactant product. 11. A process according to claim 10 , further comprising sulfating the alkoxylate surfactant product to produce an anionic ether sulfate surfactant product. 12. A process according to claim 9 , further comprising sulfating the alcohol product to produce an anionic sulfate surfactant product. 13. A process according to claim 9 , wherein the at least one olefin is ethylene and an alpha-olefin is not used. 14. A process according to claim 9 , wherein the at least one olefin is an olefin mixture. 15. A process according to claim 14 , wherein the olefin mixture includes olefins with vinyl groups, olefins with vinylidene groups, and olefins with vinylene groups. 16. A process according to claim 9 , further comprising use of a rhodium catalyst with an organophosphorus ligand in the hydroformylating step (3).
by oxo-reactions · CPC title
with hydrogen or hydrogen-containing gases · CPC title
Organic complexes · CPC title
Sulfonic acid esters · CPC title
containing only one sulfo group · CPC title
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