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Patent US5158652A successfully refreshed from Google Patents.
US5158652A
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US
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Process for the separation of tert. butyl ethyl ether from mixtures
Assignee: IFP Energies nouvelles
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Filing: 1991-04-09
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Granted: 1992-10-27
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Expires: 2011-04-09
Abstract
Abstract For the separation of tert. butyl ethyl ether from mixtures with ethanol, there are provided two distillation stages, the first being carried out at a pressure p 1 equal to or higher than 1 bar, the second at a pressure p 2 below p 1 by a value Δp or 0.5 to 12 bars, p 2 then being 0.5 to 10 bars. The second column distillate is partly supplied as reflux to the head of the second column and is in part recycled to the head of the first column. The purified TBEE is collected at the bottom of the first column and the purified ethanol at the bottom of the second column. This separation process can be integrated into a TBEE production unit comprising etherification by ethanol of the isobutylene contained in a C 4 fraction from a catalytic cracking or steam cracking stage. The ethanol separated from the TBEE is then recycled to the etherification zone.
Inventors
- 👤 Annick Pucci
- 👤 Paul Mikitenko
- 👤 Massimo Zuliani
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 21:10
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C41/34; C07C41/40; C07C41/42; C07C29/00; C07C29/74; C07C29/76; C07C29/80; Y; Y10; Y10S; Y10S203/00; Y10S203/06
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
262 words
A process for the separation of tert. butyl ethyl ether (TBEE) from mixtures thereof with ethanol, said mixtures, upon distillation form azeotropes of the tert. butyl ethyl ether and the ethanol which azeotropes have pressure-dependent compositions, said process comprising: a) introducing a charge essentially constituted by a mixture of tert. butyl ethyl ether and ethanol into a first distillation column operating under a pressure p 1 equal to or higher than 1 bar and at a temperature ranging between a bottoms temperature of 78° to 180° C. and a head temperature of 67° to 160° C., b) expanding resultant distillate leaving the head of said first column, said distillate having a composition close to that of the azeotrope at said pressure p 1 to a pressure p 2 of 0.5 to 10 bars and lower than p 1 by a value Δp of 0.5 to 12 bars, before introducing said distillate into a second distillation column operating at said pressure p 2 and at a temperature ranging between a bottoms temperature of 60° to 150° C. and a head temperature of 50° to 130° C., c) condensing resultant distillate leaving the head of said second column, said distillate having a composition close to the composition of the azeotrope at said pressure p 2 , and partly supplying resultant condensate to the head of the second column and partly recycling said condensate to the head of the first column, d) collecting resultant purified TBEE at the bottom of the first column, and e) collecting purified ethanol at the bottom of the second column.
Claim 2
Dependent Claim
262 words
A process for the separation of tert. butyl ethyl ether (TBEE) from mixtures thereof with ethanol, said mixtures, upon distillation form azeotropes of the tert. butyl ethyl ether and the ethanol which azeotropes have pressure-dependent compositions, said process comprising: a) introducing a charge essentially constituted by a mixture of tert. butyl ethyl ether and ethanol into a first distillation column operating under a pressure p 1 equal to or higher than 1 bar and at a temperature ranging between a bottoms temperature of 78° to 180° C. and a head temperature of 67° to 160° C., b) expanding resultant distillate leaving the head of said first column, said distillate having a composition close to that of the azeotrope at said pressure p 1 to a pressure p 2 of 0.5 to 10 bars and lower than p 1 by a value Δp of 0.5 to 12 bars, before introducing said distillate into a second distillation column operating at said pressure p 2 and at a temperature ranging between a bottoms temperature of 60° to 150° C. and a head temperature of 50° to 130° C., c) condensing resultant distillate leaving the head of said second column, said distillate having a composition close to the composition of the azeotrope at said pressure p 2 , and partly supplying resultant condensate to the head of the second column and partly recycling said condensate to the head of the first column, d) collecting resultant purified TBEE at the bottom of the first column, and e) collecting purified ethanol at the bottom of the second column.
Claim 3
Dependent Claim
16 words
A process according to claim 1, wherein the charge comprises 5 to 50% by weight ethanol.
Claim 4
Dependent Claim
16 words
A process according to claim 1, wherein the charge comprises 10 to 30% by weight ethanol.
Claim 5
Dependent Claim
37 words
A process according to claim 1, wherein the pressure p 1 is 2.5 to 15 bars and the pressure p 2 is lower than the pressure p 1 by a value Δp of 2 to 10 bars.
Claim 6
Dependent Claim
108 words
A process according to claim 1, wherein the charge results from a production of TBEE by etherification with ethanol of isobutylene contained in a C 4 fraction from a steam or catalytic cracking stage and said charge contains, apart from TBEE and ethanol, very small proportions of dimers of isobutylene, tert. butyl alcohol, diethyl ether and C 5 hydrocarbons, said isobutylene dimers being collected at the bottom of the first column mixed with TBEE, the said tert. butyl alcohol being collected at the bottom of the second column mixed with ethanol, said diethyl ether and said C 5 hydrocarbons passing out of the head of the first column.
Claim 7
Dependent Claim
21 words
A process according to claim 5, wherein the charge contains approximately 80% by weight TBEE and approximately 20% by weight ethanol.
Claim 8
Dependent Claim
156 words
A process for the production of tert. butyl ethyl ether (TBEE) by etherification with ethanol of isobutylene contained in a C 4 fraction from a catalytic or steam cracking stage, in which, in a reaction zone A, contacting takes place, under reaction conditions, between ethanol and said C 4 fraction, whereby the product from said reaction zone A mainly containing TBEE, ethanol, C 4 hydrocarbons other than isobutylene and, as impurities, unreacted isobutylene, isobutylene dimers, tert. butyl alcohol, diethyl ether and C 5 hydrocarbons is supplied to a distillation zone B having a head zone and a bottom zone, in which are separated, at the head zone, the C 4 hydrocarbons including the unreacted isobutylene, and at the bottom zone, a mixture of TBEE, ethanol and other impurities, and said mixture is supplied to a separation zone C, wherein said mixture is separated in said separation zone C in accordance with the process of claim 1.
Claim 9
Dependent Claim
22 words
A process according to claim 7, wherein the purified ethanol from the separation zone C is recycled to the reaction zone A.
Claim 10
Dependent Claim
51 words
A process according to claim 7, wherein in order to remove traces of diethylether and hydrocarbon, a purge is carried out on the distillate of the first column or on the distillate of the second column of the separation zone C, resultant purge stream being recycled to the distillation zone B.
Claim 11
Dependent Claim
173 words
A process for the production of tert. butyl ethyl ether (TBEE) by etherification with ethanol of isobutylene contained in a C 4 fraction catalytic or steam cracking stage, in which, in a reaction zone A, contacting takes place, under reaction conditions, between ethanol and said C 4 fraction, whereby the product from said reaction zone A mainly containing TBEE, ethanol, C 4 hydrocarbons other than isobutylene and, as impurities, unreacted isobutylene, isobutylene dimers, tert. butyl alcohol, diethyl ether and C 5 hydrocarbons is supplied to a reactive distillation zone B' having a head zone and a bottom zone, ethanol is introduced for eliminating unreacted isobutylene and forming additional ethyl tert. butyl ether, in which reactive distillation zone are separated, at the head zone, the C 4 hydrocarbons and any residual unreacted isobutylene, and at the bottom zone, a mixture of TBEE, ethanol and other impurities, and said mixture is supplied to a separation zone C, wherein said mixture is separated in said separation zone C in accordance with the process of claim 1.
Claim 12
Dependent Claim
22 words
A process according to claim 10, wherein the purified ethanol from the separation zone C is recycled to the distillation zone B'.
Claim 13
Dependent Claim
191 words
In a process for the separation of tert. butyl ethyl ether from mixtures thereof with ethanol, said mixtures, upon distillation, forming azeotropes of the tert. butyl ethyl ether and the ethanol, which azeotropes have pressure-dependent compositions, the steps comprising: a) introducing a charge essentially constituted by a mixture of tert. butyl ethyl ether and ethanol into a first distillation column operating under a pressure p 1 equal to or higher than 1 bar and at a temperature ranging between a bottoms temperature of 78° to 180° C. and a head temperature of 67° to 160° C. and recovering a distillate having a composition close to that of the respective azeotrope at said pressure p 1 , b) expanding resultant distillate leaving the head of said first column to a pressure p 2 of 0.5 to 10 bars and lower than p 1 by a value Δp of 0.5 to 12 bars, and c) introducing resultant expanded distillate into a second distillation column operating at said pressure p 2 and at a temperature ranging between a bottoms temperature of 60° to 150° C. and a head temperature of 50° to 130° C.
Claim 14
Dependent Claim
191 words
In a process for the separation of tert. butyl ethyl ether from mixtures thereof with ethanol, said mixtures, upon distillation, forming azeotropes of the tert. butyl ethyl ether and the ethanol, which azeotropes have pressure-dependent compositions, the steps comprising: a) introducing a charge essentially constituted by a mixture of tert. butyl ethyl ether and ethanol into a first distillation column operating under a pressure p 1 equal to or higher than 1 bar and at a temperature ranging between a bottoms temperature of 78° to 180° C. and a head temperature of 67° to 160° C. and recovering a distillate having a composition close to that of the respective azeotrope at said pressure p 1 , b) expanding resultant distillate leaving the head of said first column to a pressure p 2 of 0.5 to 10 bars and lower than p 1 by a value Δp of 0.5 to 12 bars, and c) introducing resultant expanded distillate into a second distillation column operating at said pressure p 2 and at a temperature ranging between a bottoms temperature of 60° to 150° C. and a head temperature of 50° to 130° C.
Claim 15
Dependent Claim
143 words
A process for the separation of tert. butyl ethyl ether (TBEE) from mixtures thereof with ethanol, said process comprising conducting a first distillation in a first distillation column operating under a pressure p 1 , and recovering from said first distillation column a distillate having a composition of substantially an azeotropic composition of the tert. butyl ethyl ether and the ethanol at said pressure p 1 ; and passing resultant distillate to a second distillation column operating under a pressure p 2 which is lower than p 1 by a value of at least 0.5 bars, and recovering from said second distillation column, a distillate having a composition of substantially the azeotropic composition of the tert. butyl ether and the ethanol at said pressure p 2 ; and recycling the latter distillate to at least one of said first and second distillation columns.
Claim 16
Dependent Claim
143 words
A process for the separation of tert. butyl ethyl ether (TBEE) from mixtures thereof with ethanol, said process comprising conducting a first distillation in a first distillation column operating under a pressure p 1 , and recovering from said first distillation column a distillate having a composition of substantially an azeotropic composition of the tert. butyl ethyl ether and the ethanol at said pressure p 1 ; and passing resultant distillate to a second distillation column operating under a pressure p 2 which is lower than p 1 by a value of at least 0.5 bars, and recovering from said second distillation column, a distillate having a composition of substantially the azeotropic composition of the tert. butyl ether and the ethanol at said pressure p 2 ; and recycling the latter distillate to at least one of said first and second distillation columns.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1995-10-27 | 1996-04-27 | 1996-10-27 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1999-10-27 | 2000-04-27 | 2000-10-27 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2003-10-27 | 2004-04-27 | 2004-10-27 | $7700.00 | Window Closed / Lapsed |