RECYCLED CONTENT OXO PRODUCTS
Recycled content oxo products are produced using a process and system that applies physical and/or credit-based recycled content from one or more feed materials to the oxo products produced from the feed materials.
1 . A process for producing an oxo product or a derivative thereof having recycled content, the process comprising:
(a) carbon reforming a hydrocarbon containing feed to thereby produce a first syngas;
(b) hydroformylating a C2 to C24 olefin with at least a portion of the first syngas to thereby produce a first oxo product; and
(c) subjecting at least a portion of the first oxo product to at least one additional reaction with an additional reactant to thereby produce a second oxo product,
wherein the second oxo product comprises recycled content from one or more of the following sources: (i) waste plastic, (ii) a recycled content syngas (r-syngas), and (iii) a recycled content additional reactant.
2 . A system or package comprising: an oxo product and an identifier associated with the oxo product, wherein the identifier is a representation that the oxo product has recycled content or is made from a source having recycled content.
3 . The process claim 1 , wherein the additional reactant comprises a recycled content additional reactant (r-reactant).
4 . The process of claim 1 , wherein the r-reactant comprises recycled content dimethyl terephthalate (r-DMT), recycled content ethylene glycol (r-EG).
5 . The process claim 1 , wherein the additional reactant is a sustainable reactant (s-reactant).
6 . The process of claim 1 , wherein the oxo product comprises recycled content obtained directly and/or indirectly from waste plastic subjected to carbon reforming.
7 . The process of claim 1 , wherein the olefin is a C2 olefin and the first oxo product is a C3 aldehyde.
8 . The process of claim 1 , wherein the olefin is a C3 olefin and the first oxo product is a C4 aldehyde.
9 . The process of claim 1 ; system, wherein the second oxo product includes one or more of the following compounds: n-propanol, n-propyl acetate, glycol ether, n-propyl propionate, cellulose acetate propionate, propionic acid, and propionic anhydride, 2-ethylhexanol, 2-ethylhexaldehyde, 2-ethylhexylacid, tri(ethylene glycol)bis(2-ethanolhexanoate), 2-ethylhexanol acetate, dipropylene glycol dibenzoate, bis(2-ethylhexyl) maleate, bis(2-ethylhexyl) terephthalate, dioctyl phthalate, bis(2-ethylhexyl) adipate, oxydiethylene dibenzoate, tris(2-ethylhexyl)trimellitate, dibutylterephthalate, methyl n-amyl ketone (MAK), n-butyric acid, normal butranitrile, butyric anhydride, cellulose acetate butyrate, n-butanol, n-butyl propionate, n-butyl acetate, n-butyraldehyde, ethylene glycol monobutyl ether, diethylene glycol monobutyl ether, ethylene glycol monopropyl ether, ethylene glycol dipropyl ether, ethylene glycol 2-ethylhexyl ether, glycol ether esters (ethylene glycol monobutyl ether ester, diethylene glycol monobutyl ether ester, and diethylene glycol monoethyl acetate), ketone, methyl isoamyl neopentyl glycol, 2,2,4-trimethyl-1,3-pentanediol monoisobutyrate, 2,2,4-trimethyl-1,3-pentanediol diisobutyrate, 2,2,4-trimethyl-1,3-pentanediol, isobutyl isobutyrate, isobutyl alcohol, isobutyl acetate, 2,2,4,4-tetramethyl-1,3-cyclobutanediol, isobutyric anhydride, isobutyronitrile, and methyl isopropyl ketone, and copolyester.
10 . The process claim 1 , wherein the additional reactant has recycled content or is sustainable.
11 . The process of claim 1 , further comprising carbon reforming a recycled content hydrocarbon feed (r-HC feed) to provide the r-syngas.
12 . The process of claim 1 , wherein the carbon reforming comprises partial oxidation gasification, or catalytic reforming, or steam reforming, or plasma gasification.
13 . The process of claim 1 , wherein the carbon reforming produces a recycled content hydrogen (r-H2) and further comprising hydrogenating at least a portion of the oxo product with r-H2.
14 . The process of claim 1 , wherein the olefin is a recycled content olefin (r-olefin) formed by pyrolysis of waste plastic, methanol, or cracking of hydrocarbons.
15 . The process, wherein the oxo product or derivative is an alcohol, a carboxylic acid, a ketone, an ester, an amide, an ether, an amine, an olefin (alkene), or a paraffin (alkane).
16 . The process of claim 1 , wherein the oxo product comprises physical recycled content from one or more of the source materials and/or credit-based recycled content from one or more of the source materials.
17 . The process of claim 1 , wherein the oxo product comprises recycled content from the r-syngas, or physical recycled content from the r-syngas, or credit-based recycled content from the r-syngas or recycled content from the r-H2, or physical recycled content from the r-H2 or credit-based recycled content from the r-H2, or recycled content from the r-reactant or physical recycled content from the r-reactant, or a combination.
18 . The process of claim 1 , wherein the carbon reforming, hydroformylating and additional reactions are carried out in an oxo product production facility, wherein at least one of the source materials providing recycled content to the oxo product is produced in a remote source facility that is located at least 0.5, 1, 5, 10, 100, 500, 1000 or 10000 miles from the oxo product production facility or a co-located source facility located within 5, 1, 0.5, or 0.25 miles of the oxo product production facility.
19 . The process of claim 1 , wherein the oxo product comprises credit-based recycled content from the at least one source material produced in the remote source facility.
20 . The process of claim 1 , further comprising apply credit-based recycled content to the oxo product from the one or more source materials.