IP Library Granted Patent US 12,296,288
Granted Patent B2
US 12,296,288 · App. 18/020,873 · Granted May 13, 2025

Multi-component mixture separation system

Inventors: Sung Kyun Kim (Daejeon, KR); Sung Kyu Lee (Daejeon, KR); Tae Woo Kim (Daejeon, KR)
Assignee: LG Chem, Ltd.
B01D3/141B01D3/008B01D3/143B01D3/32B01D5/0063B01D17/02
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 12,296,288
App. No.
18/020,873
Granted
May 13, 2025
Kind
B2
Abstract

The present disclosure provides a multi-component mixture separation system including a distillation column including a first section and a second section separated by a partition wall, and a phase separator receiving a lower discharge stream of the second section and separating the stream into an aqueous phase and an oil phase, and refluxing a portion of the separated aqueous phase or oil phase to the first section, in which the first section includes a chimney tray provided on an upper portion, and the first section is fed with a feed stream containing three or more components to separate high-boiling point component to a lower portion, and a gaseous component moves to the second section.

Claims (17)

1. A multi-component mixture separation system, comprising:

a distillation column including a first section and a second section separated by a partition wall; and

a phase separator receiving a lower discharge stream of the second section and separating the lower discharge stream into an aqueous phase and an oil phase, and refluxing a portion of the separated aqueous phase or oil phase to the first section,

wherein the lower discharge stream is discharged from a bottom of the distillation column,

wherein the first section includes a chimney tray provided on an upper portion of the first section, and

wherein the first section is supplied with a feed stream containing three or more components, and the first section is configured to separate the feed stream into a gaseous component and a high boiling point component such that the high boiling point component descends to a lower portion of the first section and the gaseous component moves to the second section.

2. The multi-component mixture separation system of claim 1 , wherein the partition wall extends upwardly from a lower end of the distillation column.

3. The multi-component mixture separation system of claim 1 , wherein a stream refluxed from the phase separator to the first section is fed to a position higher than a height to which the feed stream is fed.

4. The multi-component mixture separation system of claim 1 , wherein the chimney tray is formed to correspond to an upper area of the first section partitioned by the partition wall.

5. The multi-component mixture separation system of claim 1 , further comprising:

a liquid distribution device provided under the chimney tray.

6. The multi-component mixture separation system of claim 5 , wherein a stream refluxed from the phase separator to the first section is refluxed to a position between the chimney tray and the liquid distribution device.

7. The multi-component mixture separation system of claim 5 , wherein the feed stream is fed to a position lower than the liquid distribution device.

8. The multi-component mixture separation system of claim 1 , wherein the second section of the distillation column separates a low-boiling point component to an upper portion, feeds the lower discharge stream to the phase separator, and then separates a medium-boiling point component from any one or more of the aqueous phase and the oil phase separated in the phase separator.

9. The multi-component mixture separation system of claim 1 , wherein the phase separator refluxes a portion of the separated aqueous phase to the first section of the distillation column.

10. The multi-component mixture separation system of claim 1 , wherein the feed stream is crude hydroxypivaldehyde containing hydroxypivaldehyde and iso-butylaldehyde.

11. The multi-component mixture separation system of claim 10 , wherein the first section of the distillation column separates hydroxypivaldehyde to a lower portion, and the second section separates iso-butylaldehyde to an upper portion.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 10, 2023
From: KIM, SUNG KYUN; LEE, SUNG KYU; KIM, TAE WOO
To: LG CHEM, LTD.
Reel/Frame 062661/0780 →
Priority Claims (1)
KR 10-2021-0122586 · Sep 14, 2021 · national
Continuity (1)
Related Publication 20240299859A1 · Sep 12, 2024
References Cited (47)
US 5709780A · Ognisty et al. · 1998 [cited by applicant]
US 5755933A · Ognisty et al. · 1998 [cited by applicant]
US 6930206B1 · Groten · 2005 [cited by examiner]
US 7014833B2 · Groten · 2006 [cited by examiner]
US 7026517B2 · Groten · 2006 [cited by examiner]
US 7030277B2 · Groten · 2006 [cited by examiner]
US 7358388B2 · Woelfert · 2008 [cited by examiner]
US 7410555B2 · Groten · 2008 [cited by examiner]
US 8088944B2 · Woelfert · 2012 [cited by examiner]
US 10377690B1 · Owens · 2019 [cited by examiner]
US 10399004B2 · Hoyme · 2019 [cited by examiner]
US 10486080B2 · Choo et al. · 2019 [cited by applicant]
US 10526545B2 · Eizenga · 2020 [cited by examiner]
US 10792583B2 · Schulz · 2020 [cited by examiner]
US 10835837B2 · Hoyme · 2020 [cited by examiner]
US 11261150B2 · Rolez · 2022 [cited by examiner]
US 20040204614A1 · Groten · 2004 [cited by examiner]
US 20040210090A1 · Groten · 2004 [cited by examiner]
US 20040210091A1 · Groten · 2004 [cited by examiner]
US 20040210092A1 · Groten · 2004 [cited by examiner]
US 20040210093A1 · Groten · 2004 [cited by examiner]
US 20060135810A1 · Wolfert · 2006 [cited by examiner]
US 20070015934A1 · Wolfert · 2007 [cited by examiner]
US 20180065061A1 · Hoyme · 2018 [cited by examiner]
US 20180119023A1 · Eizenga · 2018 [cited by examiner]
US 20190247766A1 · Hoyme · 2019 [cited by examiner]
US 20190299116A1 · Schulz · 2019 [cited by examiner]
US 20210300857A1 · Rolez · 2021 [cited by examiner]
CN 103328464A · 2015 [cited by applicant]
CN 105142747A · 2018 [cited by applicant]
CN 111298471A · 2020 [cited by applicant]
JP 9136855A · 1997 [cited by applicant]
JP H09124536A · 1997 [cited by applicant]
JP 1057703A · 1998 [cited by applicant]
JP 2000239228A · 2000 [cited by applicant]
KR 100231644B1 · 1999 [cited by applicant]
KR 101092199B1 · 2011 [cited by applicant]
KR 101325821B1 · 2013 [cited by applicant]
KR 101530102B1 · 2015 [cited by applicant]
KR 1020150120500A · 2015 [cited by applicant]
KR 1020170029311A · 2017 [cited by applicant]
KR 101784456B1 · 2017 [cited by applicant]
KR 101805324B1 · 2017 [cited by applicant]
KR 1020190056738A · 2019 [cited by applicant]
KR 1020200133789A · 2020 [cited by applicant]
KR 1020210029251A · 2021 [cited by applicant]
RU 2717093C1 · 2020 [cited by applicant]