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US4191614A Expired / Lapsed US ⏱️ 0.0 years remaining

Distillation apparatus

Assignee: Cosden Technology Inc
•
Filing: 1976-03-01
•
Granted: 1980-03-04
•
Expires: 1996-03-01
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Abstract

Abstract Apparatus for the distillation of styrene from hydrocarbon feedstock incorporating a system for injection of gaseous polymerization inhibitor.

Inventors

  • 👤 James M. Watson
  • 👤 Michael E. Johnson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 07:21
CPC Classifications
B; B01; B01D; B01D3/00; B01D3/34; B01D3/343; C; C07; C07C; C07C7/00; C07C7/04; C07C7/05; Y; Y10; Y10S; Y10S203/00; Y10S203/90

Claims Analysis

Total Claims: 7
Claim 1
Independent Claim 126 words
Apparatus for the distillative purification and recovery of styrene monomer from a styrene-containing feedstock, comprising: (a) at least one distillation column for receiving said feedstock; (b) a reboiler operatively associated with each column; (c) gas injection means for introducing a gaseous inhibitor into each column; (d) gas injection means for introducing a gaseous inhibitor into each reboiler; (e) a source of gaseous inhibitor in operative communication with each of said gas injection means; (f) gas flow control means including at least one valve member intermediate said source of gaseous inhibitor and each of said gas injection means for permitting controlled simultaneous apportionment of said gaseous inhibitor between each column and each reboiler, whereby polymerization of said monomer is prevented; and, (g) means to recover said monomer.
Claim 2
Dependent Claim 126 words
Apparatus for the distillative purification and recovery of styrene monomer from a styrene-containing feedstock, comprising: (a) at least one distillation column for receiving said feedstock; (b) a reboiler operatively associated with each column; (c) gas injection means for introducing a gaseous inhibitor into each column; (d) gas injection means for introducing a gaseous inhibitor into each reboiler; (e) a source of gaseous inhibitor in operative communication with each of said gas injection means; (f) gas flow control means including at least one valve member intermediate said source of gaseous inhibitor and each of said gas injection means for permitting controlled simultaneous apportionment of said gaseous inhibitor between each column and each reboiler, whereby polymerization of said monomer is prevented; and, (g) means to recover said monomer.
Claim 3
Dependent Claim 107 words
The apparatus of claim 1, wherein said apparatus comprises a distillation train including at least three columns: (a) the first of said columns being adapted to remove and collect benzene and toluene as an overhead product and deliver the bottom product of styrene, unreacted ethylbenzene, high boiling polymer, and tar to a second of said columns; (b) the second of said columns being adapted to remove and recycle said unreacted ethylbenzene as an overhead product and deliver the bottom product of crude styrene to a third of said columns; (c) the third of said columns being adapted to remove pure styrene monomer and deliver same for collection.
Claim 4
Dependent Claim 26 words
The apparatus of claim 2, wherein said gas injecting means includes an inlet for said gaseous inhibitor into the vapor space of each of said columns.
Claim 5
Dependent Claim 50 words
The apparatus of claim 2, further comprising: (a) a fourth column for receiving the bottom product of styrene and tar from said third column, said fourth column being adapted to remove and deliver pure styrene monomer as an overhead product; and (b) a reboiler operatively associated with said fourth column.
Claim 6
Dependent Claim 23 words
The apparatus of claim 4, wherein said gas injecting means includes an inlet for gaseous inhibitor into said reboiler for said fourth column.
Claim 7
Dependent Claim 24 words
The apparatus of claim 4, wherein said gas injecting means includes an inlet for gaseous inhibitor into the vapor space of said fourth column.

References Cited (Backward Citations)

US2389793A Cited
US2407861A Cited
US2473203A Cited
US3408264A Cited
US3515647A Cited
US3631214A Cited
US3904484A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-03-04 1983-09-03 1984-03-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-03-04 1987-09-03 1988-03-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-03-04 1991-09-03 1992-03-04 $7700.00 Window Closed / Lapsed

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