US4546204A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Process for the manufacture of methyl t-butyl ether
Assignee: Orica Ltd
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Filing: 1984-10-29
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Granted: 1985-10-08
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Expires: 2004-10-29
Abstract
Abstract The invention concerns a process for the manufacture of methyl t-butyl ether in which: a hydrocarbon feedstock is cracked to give an ethylene-rich stream; an isobutane-rich stream is separated from C 4 -hydrocarbon stream; the ethylene-rich stream and the isobutane-rich stream are contacted over a transhydrogenation catalyst to give a mixture comprising ethane and isobutene; the isobutene is reacted with methanol to give methyl t-butyl ether; and the residual C 4 -hydrocarbon stream is recycled either to the C 4 -hydrocarbon stream or to the cracker and the ethane is recycled to the cracker. It has been found that combining and interconnecting a hydrocarbon cracker, a transhydrogenation reactor and an etherification reactor results in an integrated, economic process for the production of methyl t-butyl ether.
Inventors
- 👤 David Parris
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 05:19
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C41/05; C07C41/06; C07C5/00; C07C5/42; C07C5/50; C07C5/52
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
236 words
A process for the manufacture of methyl t-butyl ether which process comprises the following steps: (i) cracking a hydrocarbon feedstock in a cracking facility to give an ethylene-rich stream; (ii) separating an isobutane enriched stream from a C 4 -hydrocarbon stream and optionally isomerizing the n-butane and recycling the resulting C 4 -hydrocarbon stream for separation; (iii) contacting a mixture comprising the ethylene-rich stream from step (i) and the isobutane enriched stream from step (ii) with a transhydrogenation catalyst to give a hydrocarbon mixture comprising isobutene and ethane; (iv) either first separating the hydrocarbon mixture obtained in step (iii) into a C 4 -hydrocarbon enriched stream comprising isobutene and a C 2 -hydrocarbon enriched stream comprising ethane and second reacting said C 4 -hydrocarbon enriched stream comprising isobutene with methanol to give methyl t-butyl ether and a residual C 4 -hydrocarbon stream; or first reacting said mixture obtained in step (iii) with methanol to give methyl t-butyl ether and a residual hydrocarbon stream and optionally separating the residual hydrocarbon stream into a residual C 4 -hydrocarbon stream and a C 2 -hydrocarbon enriched stream; and (v) collecting the methyl t-butyl ether and recycling the residual C 4 -hydrocarbon stream either to the C 4 -hydrocarbon stream or to the cracking facility as feedstock and recycling the C 2 -hydrocarbon enriched stream to the cracking facility or recycling the unseparated residual hydrocarbon stream to the cracking facility.
Claim 2
Dependent Claim
236 words
A process for the manufacture of methyl t-butyl ether which process comprises the following steps: (i) cracking a hydrocarbon feedstock in a cracking facility to give an ethylene-rich stream; (ii) separating an isobutane enriched stream from a C 4 -hydrocarbon stream and optionally isomerizing the n-butane and recycling the resulting C 4 -hydrocarbon stream for separation; (iii) contacting a mixture comprising the ethylene-rich stream from step (i) and the isobutane enriched stream from step (ii) with a transhydrogenation catalyst to give a hydrocarbon mixture comprising isobutene and ethane; (iv) either first separating the hydrocarbon mixture obtained in step (iii) into a C 4 -hydrocarbon enriched stream comprising isobutene and a C 2 -hydrocarbon enriched stream comprising ethane and second reacting said C 4 -hydrocarbon enriched stream comprising isobutene with methanol to give methyl t-butyl ether and a residual C 4 -hydrocarbon stream; or first reacting said mixture obtained in step (iii) with methanol to give methyl t-butyl ether and a residual hydrocarbon stream and optionally separating the residual hydrocarbon stream into a residual C 4 -hydrocarbon stream and a C 2 -hydrocarbon enriched stream; and (v) collecting the methyl t-butyl ether and recycling the residual C 4 -hydrocarbon stream either to the C 4 -hydrocarbon stream or to the cracking facility as feedstock and recycling the C 2 -hydrocarbon enriched stream to the cracking facility or recycling the unseparated residual hydrocarbon stream to the cracking facility.
Claim 3
Dependent Claim
20 words
A process according to claim 1 wherein said cracking facility is a hydrocarbon cracker designed for the production of olefins.
Claim 4
Dependent Claim
25 words
A process according to claim 1 wherein said cracking facility is a refinery cracker designed to crack crude oil for the production of petroleum products.
Claim 5
Dependent Claim
41 words
A process according to claim 1 wherein said transhydrogenation catalyst is selected from metals and oxides of metals selected from the Groups IVA, VA, VIA, VIIA, VIII, and copper, zinc, gallium, indium, germanium, tin, lead, antimony, bismuth, tellurium and mixtures thereof.
Claim 6
Dependent Claim
40 words
A process according to claim 4 wherein said transhydrogenation catalyst is selected from the metals platinum, palladium, nickel, iridium, rhodium, cobalt, rhenium, ruthenium, iron and copper oxides of the metals chromium, molybdenum, copper, tungsten, titanium and zinc, and mixtures thereof.
Claim 7
Dependent Claim
17 words
A process according to claim 5 wherein said transhydrogenation catalyst is supported on a non-acidic porous carrier.
Claim 8
Dependent Claim
21 words
A process according to claim 6 wherein said transhydrogenation catalyst is a chromium oxide catalyst supported on a non-acidic alumina carrier.
Claim 9
Dependent Claim
40 words
A process according to claim 1 wherein in step (iii) said transhydrogenation process is carried out at a temperature in the range of from 400° to 550° C. and at a pressure in the range of 1.0 to 10 atmospheres.
Claim 10
Dependent Claim
40 words
A process according to claim 1 wherein in step (iv) said reaction between methanol and isobutene to give methyl t-butyl ether is carried out by contacting a liquid phase mixture comprising methanol and isobutene with a solid phase acidic catalyst.
Claim 11
Dependent Claim
228 words
A process for the manufacture of methyl t-butyl ether which process comprises the following steps: (i) cracking a hydrocarbon feedstock in a hydrocarbon cracker to give an ethylene-rich stream; (ii) separating a C 4 -hydrocarbon stream into an isobutane enriched stream and an n-butane enriched stream in a de-isobutanizer unit, isomerizing the n-butane enriched stream in a catalytic isomerization reactor to give an isobutane/n-butane mixture, and recycling the isobutane/n-butane mixture to the deisobutanizer unit; (iii) reacting a mixture comprising the ethylene-rich stream from step (i) and the isobutane enriched stream from step (ii) over a chromium oxide on alumina transhydrogenation catalyst at a temperature in the range from 400° to 550° C. and at a pressure in the range of from 1.0 to 10 atmospheres to give a hydrocarbon mixture comprising isobutene and ethane; (iv) separating the hydrocarbon mixture from step (iii) into a C 4 -hydrocarbon enriched stream comprising isobutene and a C 2 -hydrocarbon enriched stream comprising ethane in a debutanizer column and reacting said C 4 -hydrocarbon enriched stream with methanol in the liquid phase over an acidic solid phase catalyst to give methyl t-butyl ether and a residual C 4 -hydrocarbon stream; and (v) recycling the C 2 -hydrocarbon enriched stream to the hydrocarbon cracker, collecting the methyl t-butyl ether, and recycling the residual C 4 -hydrocarbon stream to the C 4 -hydrocarbon stream.
Claim 12
Dependent Claim
228 words
A process for the manufacture of methyl t-butyl ether which process comprises the following steps: (i) cracking a hydrocarbon feedstock in a hydrocarbon cracker to give an ethylene-rich stream; (ii) separating a C 4 -hydrocarbon stream into an isobutane enriched stream and an n-butane enriched stream in a de-isobutanizer unit, isomerizing the n-butane enriched stream in a catalytic isomerization reactor to give an isobutane/n-butane mixture, and recycling the isobutane/n-butane mixture to the deisobutanizer unit; (iii) reacting a mixture comprising the ethylene-rich stream from step (i) and the isobutane enriched stream from step (ii) over a chromium oxide on alumina transhydrogenation catalyst at a temperature in the range from 400° to 550° C. and at a pressure in the range of from 1.0 to 10 atmospheres to give a hydrocarbon mixture comprising isobutene and ethane; (iv) separating the hydrocarbon mixture from step (iii) into a C 4 -hydrocarbon enriched stream comprising isobutene and a C 2 -hydrocarbon enriched stream comprising ethane in a debutanizer column and reacting said C 4 -hydrocarbon enriched stream with methanol in the liquid phase over an acidic solid phase catalyst to give methyl t-butyl ether and a residual C 4 -hydrocarbon stream; and (v) recycling the C 2 -hydrocarbon enriched stream to the hydrocarbon cracker, collecting the methyl t-butyl ether, and recycling the residual C 4 -hydrocarbon stream to the C 4 -hydrocarbon stream.
Claim 13
Dependent Claim
218 words
A process for the manufacture of methyl t-butyl ether which process comprises the following steps: (i) cracking a hydrocarbon feedstock in hydrocarbon cracker to give an ethylene-rich stream; p1 (ii) separating a C 4 -hydrocarbon stream into an isobutane enriched stream and an n-butane enriched stream in a deisobutanizer unit and recycling the n-butane enriched stream to the hydrocarbon cracker for use as feedstock; (iii) reacting a mixture comprising the ethylene-rich stream from step (i) and the isobutane enriched stream from step (ii) over a chromium oxide on alumina transhydrogenation catalyst at a temperature in the range from 400° to 550° C. and at a pressure in the range of from 1.0 to 10 atmospheres to give a hydrocarbon mixture comprising isobutene and ethane; (iv) separating the hydrocarbon mixture from step (iii) into a C 4 -hydrocarbon enriched stream comprising isobutene and a C 2 -hydrocarbon enriched stream comprising ethane in a debutanizer column and reacting said C 4 -hydrocarbon enriched stream with methanol in the liquid phase over an acidic solid phase catalyst to give methyl t-butyl ether and a residual C 4 -hydrocarbon stream; and (v) recycling the C 2 -hydrocarbon enriched stream to the hydrocarbon cracker, collecting the methyl t-butyl ether, and recycling the residual C 4 -hydrocarbon stream to the C 4 -hydrocarbon stream.
Claim 14
Dependent Claim
218 words
A process for the manufacture of methyl t-butyl ether which process comprises the following steps: (i) cracking a hydrocarbon feedstock in hydrocarbon cracker to give an ethylene-rich stream; p1 (ii) separating a C 4 -hydrocarbon stream into an isobutane enriched stream and an n-butane enriched stream in a deisobutanizer unit and recycling the n-butane enriched stream to the hydrocarbon cracker for use as feedstock; (iii) reacting a mixture comprising the ethylene-rich stream from step (i) and the isobutane enriched stream from step (ii) over a chromium oxide on alumina transhydrogenation catalyst at a temperature in the range from 400° to 550° C. and at a pressure in the range of from 1.0 to 10 atmospheres to give a hydrocarbon mixture comprising isobutene and ethane; (iv) separating the hydrocarbon mixture from step (iii) into a C 4 -hydrocarbon enriched stream comprising isobutene and a C 2 -hydrocarbon enriched stream comprising ethane in a debutanizer column and reacting said C 4 -hydrocarbon enriched stream with methanol in the liquid phase over an acidic solid phase catalyst to give methyl t-butyl ether and a residual C 4 -hydrocarbon stream; and (v) recycling the C 2 -hydrocarbon enriched stream to the hydrocarbon cracker, collecting the methyl t-butyl ether, and recycling the residual C 4 -hydrocarbon stream to the C 4 -hydrocarbon stream.
Claim 15
Dependent Claim
228 words
A process for the manufacture of methyl t-butyl ether which process comprises the following steps: (i) separating hydrogen from a refinery dry gas stream obtained from a refinery hydrocarbon cracking process to give an ethylene enriched stream and recycling the hydrogen for refinery use; (ii) separating a C 4 -hydrocarbon stream obtained from natural gas or refinery operations into an isobutane enriched stream and an n-butane enriched stream in a deisobutanizer unit and recycling the n-butane enriched stream for refinery use; (iii) reacting a mixture comprising the ethylene enriched stream from step (i) and the isobutane enriched stream from step (ii) over a chromium oxide on alumina transhydrogenation catalyst at a temperature in the range from 400° to 550° C. and at a pressure in the range from 1.0 to 10 atmospheres to give a hydrocarbon mixture comprising isobutene and ethane; (iv) separating the hydrocarbon mixture from step (iii) into a C 4 -hydrocarbon enriched stream comprising isobutene and a C 2 -hydrocarbon enriched stream comprising ethane in a debutanizer column and reacting said C 4 -hydrocarbon enriched stream with methanol in the liquid phase over an acidic solid phase catalyst to give methyl t-butyl ether and a residual C 4 -hydrocarbon stream; and (v) collecting the methyl t-butyl ether and recycling the C 2 -hydrocarbon enriched stream and the residual C 4 -hydrocarbon stream for refinery use.
Claim 16
Dependent Claim
228 words
A process for the manufacture of methyl t-butyl ether which process comprises the following steps: (i) separating hydrogen from a refinery dry gas stream obtained from a refinery hydrocarbon cracking process to give an ethylene enriched stream and recycling the hydrogen for refinery use; (ii) separating a C 4 -hydrocarbon stream obtained from natural gas or refinery operations into an isobutane enriched stream and an n-butane enriched stream in a deisobutanizer unit and recycling the n-butane enriched stream for refinery use; (iii) reacting a mixture comprising the ethylene enriched stream from step (i) and the isobutane enriched stream from step (ii) over a chromium oxide on alumina transhydrogenation catalyst at a temperature in the range from 400° to 550° C. and at a pressure in the range from 1.0 to 10 atmospheres to give a hydrocarbon mixture comprising isobutene and ethane; (iv) separating the hydrocarbon mixture from step (iii) into a C 4 -hydrocarbon enriched stream comprising isobutene and a C 2 -hydrocarbon enriched stream comprising ethane in a debutanizer column and reacting said C 4 -hydrocarbon enriched stream with methanol in the liquid phase over an acidic solid phase catalyst to give methyl t-butyl ether and a residual C 4 -hydrocarbon stream; and (v) collecting the methyl t-butyl ether and recycling the C 2 -hydrocarbon enriched stream and the residual C 4 -hydrocarbon stream for refinery use.
References Cited (Backward Citations)
US4329516A
Cited
US4423251A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1988-10-07 | 1989-04-08 | 1989-10-08 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1992-10-07 | 1993-04-08 | 1993-10-08 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1996-10-07 | 1997-04-08 | 1997-10-08 | $7700.00 | Window Closed / Lapsed |