Methods for making linear internal olefins from mixtures of linear and branched olefins
US-2024051900-A1 · Feb 15, 2024 · US
US9908837B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9908837-B2 |
| Application number | US-201414769850-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 13, 2014 |
| Priority date | Mar 15, 2013 |
| Publication date | Mar 6, 2018 |
| Grant date | Mar 6, 2018 |
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Polymers, particularly those used in pressure-sensitive adhesives, are prepared from a mixture of structural isomers of a secondary alkyl (meth)acrylate monomer. The mixture is made by dehydrating a biobased C 2 -C 22 alcohol with a first acid catalyst using a continuous process to form a mixture of olefins, and reacting (meth)acrylic acid with at least some of the mixture of olefins in the presence of a second acid catalyst. The adhesives are characterized by exhibiting an overall balance of adhesive and cohesive characteristics, and containing biobased material.
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What is claimed is: 1. A method of making a mixture of structural isomers of a secondary alkyl(meth)acrylate of Formula (I): wherein: R 1 and R 2 are each independently a C 1 to C 20 saturated linear alkyl group; the sum of the number of carbons in R 1 and R 2 is 2 to 21; and R 3 is H or CH 3 ; wherein the method comprises: dehydrating a biobased C 2 -C 22 alcohol derived from at least one plant oil with a first acid catalyst using a continuous process, thereby forming a mixture of olefins, the first acid catalyst comprising a sulfonated styrene divinylbenzene copolymer; and reacting (meth)acrylic acid with at least some of the mixture of olefins in the presence of a second acid catalyst comprising a sulfonated styrene divinylbenzene copolymer. 2. The method of claim 1 wherein the first acid catalyst comprises a cation exchange resin. 3. The method of claim 1 wherein the mixture of olefins comprises between 80% and 100% by weight biobased olefins, as determined using ASTM D6866-12. 4. The method of claim 1 wherein the dehydrating occurs at a temperature of 150° C. to 190° C. 5. The method of claim 1 wherein the C 2 -C 22 alcohol comprises a C 8 alcohol, a C 10 alcohol, or a C 12 alcohol. 6. The method of claim 1 wherein the dehydrating is performed in a continuous reactor at a temperature of 150° C. to 190° C. and at a constant weight hourly space velocity (WHSV) of 0.5 h −1 to 10 h −1 , wherein the WHSV is a ratio of mass flow of the C 2 -C 22 alcohol entering the system per hour to the mass of the first acid catalyst. 7. The method of claim 1 wherein the dehydrating is performed in a continuous reactor at a temperature of 150° C. to 190° C. and combination of the mixture of olefins and water is produced at a rate of 0.5 g h −1 to 10 g h −1 per gram of the first acid catalyst.
by elimination of water · CPC title
Ion-exchange resins · CPC title
by reacting carboxylic acids or symmetrical anhydrides onto unsaturated carbon-to-carbon bonds · CPC title
sulfonated · CPC title
Homopolymers or copolymers of acrylic acid esters · CPC title
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