PROCESS AND SYSTEMS FOR OBTAINING 1,4-BUTANEDIOL FROM FERMENTATION BROTHS
A process of purifying 1,4-butanediol (1,4-BDO) from a fermentation broth including separating solid materials, salts and water, and subjecting the resulting material to a two, three or four column distillation system, that can include a wiped film evaporator to produce a purified 1,4-butanediol.
1 . A process of purifying 1,4-butanediol (1,4-BDO) comprising:
(a) subjecting a crude 1,4-BDO mixture to a first column distillation procedure to remove materials with a boiling point lower than 1,4-BDO from the crude 1,4-BDO mixture to produce a first 1,4-BDO-containing product stream; and
(b) subjecting the first 1,4-BDO-containing product stream to a second column distillation procedure to remove materials with boiling points higher than 1,4-BDO as a first high-boilers stream, to produce a purified 1,4-BDO product, wherein the purified 1,4-BDO product is collected from a side-draw of the second column distillation procedure.
2 . The process of claim 1 , further comprising (c) subjecting the first high-boilers stream to wiped-film evaporation (WFE) to produce a first WFE distillate and subjecting the first WFE distillate to step (b).
3 . The process of claim 1 further comprising (d) subjecting the first 1,4-BDO-containing product stream, prior to performing step (b), to an intermediate column distillation procedure to remove materials with boiling points higher than 1,4-BDO as a second high-boilers stream.
4 . The process of claim 3 , further comprising (c) subjecting the second high-boilers stream to wiped-film evaporation (WFE) producing a second WFE distillate and subjecting the second WFE distillate to step (d).
5 . The process of claim 3 further comprising (e) treating the first 1,4-BDO-containing product stream with a hydrogenation reaction prior to performing step (b).
6 . The process of claim 1 further comprising (f) treating the purified 1,4-BDO product with a hydrogenation reaction.
7 . The process of claim 1 wherein the crude 1,4-BDO mixture is at least 50% (w/w), 60% (w/w), 70% (w/w), 80% (w/w), 85% (w/w) or 90% (w/w) 1,4-BDO.
8 . The process of claim 1 , wherein the purified 1,4-BDO product is greater than 90% (w/w), 91% (w/w), 92% (w/w), 93% (w/w), 94% (w/w), 95% (w/w), 96% (w/w), 97%, (w/w) 98% (w/w), 99% (w/w), 99.1% (w/w), 99.2% (w/w), 99.3% (w/w), 99.4% (w/w), 99.5% (w/w), 99.6% (w/w), 99.7% (w/w), 99.8% (w/w) or 99.9% (w/w), 1,4-BDO.
9 . The process of claim 1 , wherein recovery of 1,4-BDO in the purified 1,4-BDO product from the crude 1,4-BDO mixture is greater than 40%, 50%, 60%, 70%, 80%, 90%, 95%, 96%, 97%, 98% or 99%.
10 . The process of claim 1 , wherein the purified 1,4-BDO product collected from the side draw is in a vapor phase.
11 . The process of claim 1 , wherein the first column distillation procedure and second column distillation procedures are each performed at pressures equal to or less than atmospheric pressure.
12 . The process of claim 11 , wherein the pressure of the first column distillation procedure differs from the pressure of the second distillation procedure.
13 . The process of claim 1 further comprising culturing a modified non-naturally occurring organism to produce a 1,4-BDO in a fermentation broth, subjecting the fermentation broth to a separation procedure to obtain a separated 1,4-BDO product, and subjecting the separated 1,4-BDO product to water removal and salt removal to produce the crude 1,4-BDO mixture, wherein the separation procedure consists of a first filtration and a second filtration, wherein the first filtration is microfiltration or ultrafiltration, and wherein the second filtration is nanofiltration.
14 . The process of claim 13 , further comprising subjecting the crude 1,4-BDO mixture to a polishing ion exchange using a polishing ion exchange resin that is an anion exchange resin.
15 . The process of claim 13 , wherein the water removal is by evaporation.
16 . The process of claim 13 , wherein the salt removal is by primary ion exchange.
17 . A system for purifying 1,4-BDO comprising:
a first distillation column receiving a crude 1,4-BDO mixture and generating a first stream of materials with boiling points lower than 1,4-BDO and a 1,4-BDO-containing product stream;
a second distillation column receiving the 1,4-BDO-containing product stream at a feed point and generating a first stream of materials with boiling points higher than 1,4-BDO, a second stream of materials with boiling points lower than 1,4-BDO, and a purified 1,4-BDO product from a side-draw; and
a wiped-film evaporator receiving the first stream of materials with boiling points higher than 1,4-BDO and generating a distillate, wherein the distillate is fed to the second distillation column.
18 . The system of claim 17 further comprising a hydrogenation reactor constructed to treat the purified 1,4-BDO product generated by the second distillation column.
19 . The system of claim 17 , wherein the side-draw is located above the feed point of the second distillation column.
20 . A system for purifying 1,4-BDO comprising:
a first distillation column receiving a crude 1,4-BDO mixture generating a first stream of materials with boiling points lower than 1,4-BDO and a first 1,4-BDO-containing product stream;
an intermediate distillation column receiving the first 1,4-BDO-containing product stream generating a first stream of materials with boiling points higher than 1,4-BDO, and a second 1,4-BDO-containing product stream;
a wiped-film evaporator receiving the first stream of materials with boiling points higher than 1,4-BDO and generating a distillate, wherein the distillate is fed to the intermediate distillation column; and
a second distillation column receiving the second 1,4-BDO-containing product stream at a feed point and generating a second stream of materials with boiling points lower than 1,4-BDO, a second stream of materials with boiling points higher than 1,4-BDO, and a purified 1,4-BDO product from a side-draw.
21 . The system of claim 19 further comprising a hydrogenation reactor constructed to treat the second 1,4-BDO-containing product stream prior to the second 1,4-BDO-containing product stream being received by the second distillation column.
22 . The system of claim 19 , wherein the side-draw is located below the feed point of the second distillation column.
23 . A process of producing a 1,4-BDO product comprising:
culturing a modified non-naturally occurring organism to produce a 1,4-BDO in a fermentation broth;
subjecting the fermentation broth to a separation procedure to obtain a separated 1,4-BDO product, wherein the separation procedure consists a first filtration and a second filtration, wherein the first filtration is microfiltration or ultrafiltration, wherein the second filtration is nanofiltration; and
subjecting the separated 1,4-BDO product to a polishing ion exchange using a polishing ion exchange resin.
24 . The process of claim 23 further comprising subjecting the separated 1,4-BDO product to water removal before subjecting the separated 1,4-BDO product to the polishing ion exchange.
25 . The process of claim 23 further comprising subjecting the separated 1,4-BDO product to primary ion exchange using a primary ion exchange resin before subjecting the separated 1,4-BDO product to the polishing ion exchange.
26 . The process of claim 25 , wherein the primary ion exchange resin comprises a cation exchange resin and a anion exchange resin.
27 . Bioderived 1,4-BDO, wherein the bioderived 1,4-BDO is produced by the process of claim 1 .
28 . The bioderived 1,4-BDO of claim 27 having a carbon-12, carbon-13 and carbon-14 isotope ratio that reflects an atmospheric carbon dioxide source.
29 . A biobased plastic, elastic fiber, polyurethane, polyester, poly-4-hydroxybutyrate or co-polymer thereof, poly(tetramethylene ether)glycol and polyurethane-polyurea copolymer comprising said bioderived 1,4-BDO from of claim 27 .
30 . The biobased plastic, elastic fiber, polyurethane, polyester, poly-4-hydroxybutyrate or co-polymer thereof, poly(tetramethylene ether)glycol and polyurethane-polyurea copolymer of claim 28 comprising at least 5%, at least 10%, at least 20%, at least 30%, at least 40%, or at least 50% bioderived 1,4-BDO.
31 . A system for purifying 1,4-BDO comprising:
a first distillation column receiving a crude 1,4-BDO mixture generating a first stream of materials with boiling points lower than 1,4-BDO and a first 1,4-BDO-containing product stream;
a first intermediate distillation column receiving the first 1,4-BDO-containing product stream generating a first stream of materials with boiling points higher than 1,4-BDO, and a second 1,4-BDO-containing product stream;
a wiped-film evaporator receiving the first stream of materials with boiling points higher than 1,4-BDO and generating a distillate, wherein the distillate is fed to the first intermediate distillation column;
a second intermediate distillation column receiving the second 1,4-BDO-containing product stream generating a second stream of materials with boiling points lower than 1,4-BDO, and a third 1,4-BDO-containing product stream; and
a second distillation column receiving the third 1,4-BDO-containing product stream at a feed point and generating a second stream of materials with boiling points higher than 1,4-BDO, and a purified 1,4-BDO product.
32 . The system of claim 31 further comprising a hydrogenation reactor constructed to treat the second 1,4-BDO-containing product stream prior to the second 1,4-BDO-containing product stream being received by the second intermediate distillation column.
33 . The system of claim 31 wherein the second distillation column further comprises a side draw, and the generated purified 1,4-BDO product is from the side draw.