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US4324924A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for removing isobutene from a C4 cut and producing methyl tert-butyl ether

Assignee: IFP Energies nouvelles
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Filing: 1980-04-24
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Granted: 1982-04-13
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Expires: 2000-04-24
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Abstract

Abstract Process for producing methyl tert-butyl ether (MTBE) by reacting methanol with the isobutene present in a C 4 cut in a proportion from 10 to 60%, wherein said cut, admixed with methanol is contacted, in a first reaction zone, with an acid catalyst in the conditions of etherification of isobutene by methanol unit 93 to 98% of the isobutene has been converted, the reaction product is fractionated under at least 10 bars to a bottom fraction consisting essentially of MTBE and a top fraction which is contacted, in a second reaction zone, with an acid catalyst, under the conditions of etherification of isobutene by methanol, until at least 99% of the initial isobutene has been converted, the resulting product is washed with water and separated into a residual C 4 cut which is discharged and an aqueous phase wherefrom methanol is recovered by distillation.

Inventors

  • 👤 Bernard Torck
  • 👤 Alaio Convers
  • 👤 Didier Duee
  • 👤 Paul Mikitenko

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 11:04
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C41/05; C07C41/06

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 289 words
A process for producing methyl tert-butyl ether and recovering a substantially isobutene- and methanol-free C 4 cut by reacting methanol with a hydrocarbon C 4 cut comprising from 10 to 60% by weight of isobutene, said process comprising the steps of: (a) contacting a mixture of methanol, said C 4 cut, and a recycle stream as hereinafter defined, in a first reaction zone, with an acid catalyst, under conditions for etherification of isobutene with methanol, and converting from 93 to 98% of isobutene, the methanol/isobutene molar ratio being maintained higher than 1:1 at the inlet and at the outlet of said first reaction zone; (b) fractionating the effluent from step (a) under a pressure of at least 10 bars, and separately recovering an overhead fraction having a methanol/isobutene molar ratio higher than 1:1 and a bottoms product fraction comprising methyl tert-butyl ether, and discharging said bottoms product fraction; (c) contacting the overhead fraction from step (b) with an acid catalyst, in a second reaction zone, under conditions for etherification of isobutene with methanol such that an overall isobutene conversion of at least 99% is effected; (d) fractionating the effluent from step (c) under a pressure of 1-9 bars, and separately recovering an overhead fraction consisting essentially of C 4 hydrocarbons and a minor proportion of methanol, and a bottoms fraction containing methanol, methyl tert-butyl ether and a minor proportion of C 4 hydrocarbons, and having a methanol/methyl tert-butyl ether molar ratio higher than 1:1, said bottoms fraction being recycled as said recycle stream to step (a); and (e) washing at least a portion of the overhead fraction from step (d) with water, and separately recovering a substantially isobutene- and methanol-free C 4 cut, and a methanol-containing aqueous wash stream.
Claim 2
Dependent Claim 289 words
A process for producing methyl tert-butyl ether and recovering a substantially isobutene- and methanol-free C 4 cut by reacting methanol with a hydrocarbon C 4 cut comprising from 10 to 60% by weight of isobutene, said process comprising the steps of: (a) contacting a mixture of methanol, said C 4 cut, and a recycle stream as hereinafter defined, in a first reaction zone, with an acid catalyst, under conditions for etherification of isobutene with methanol, and converting from 93 to 98% of isobutene, the methanol/isobutene molar ratio being maintained higher than 1:1 at the inlet and at the outlet of said first reaction zone; (b) fractionating the effluent from step (a) under a pressure of at least 10 bars, and separately recovering an overhead fraction having a methanol/isobutene molar ratio higher than 1:1 and a bottoms product fraction comprising methyl tert-butyl ether, and discharging said bottoms product fraction; (c) contacting the overhead fraction from step (b) with an acid catalyst, in a second reaction zone, under conditions for etherification of isobutene with methanol such that an overall isobutene conversion of at least 99% is effected; (d) fractionating the effluent from step (c) under a pressure of 1-9 bars, and separately recovering an overhead fraction consisting essentially of C 4 hydrocarbons and a minor proportion of methanol, and a bottoms fraction containing methanol, methyl tert-butyl ether and a minor proportion of C 4 hydrocarbons, and having a methanol/methyl tert-butyl ether molar ratio higher than 1:1, said bottoms fraction being recycled as said recycle stream to step (a); and (e) washing at least a portion of the overhead fraction from step (d) with water, and separately recovering a substantially isobutene- and methanol-free C 4 cut, and a methanol-containing aqueous wash stream.
Claim 3
Dependent Claim 44 words
A process according to claim 1, wherein the molar ratio methanol/isobutene at the inlet of the reaction zone of step (a) is selected so as to obtain a value from 3:1 to 20:1 of the corresponding ratio at the outlet of said reaction zone.
Claim 4
Dependent Claim 18 words
A process according to claim 2, wherein said ratio, at the inlet, is selected from 1.05:1 to 1.3:1.
Claim 5
Dependent Claim 26 words
A process according to claim 1, wherein a portion of the overhead fraction from step (b) is fed back to the reaction zone of step (a).
Claim 6
Dependent Claim 18 words
A process according to claim 1, wherein the pressure in step (b) is from 14 to 20 bars.
Claim 7
Dependent Claim 18 words
A process according to claim 5, wherein in step (d), the pressure is from 3 to 6 bars.
Claim 8
Dependent Claim 18 words
A process according to claim 1, wherein in step (d) the pressure is from 3 to 6 bars.
Claim 9
Dependent Claim 15 words
A process according to claim 1, wherein said water fraction is recycled to step (e).
Claim 10
Dependent Claim 21 words
A process according to claim 1, wherein in step (d), said methanol/methyl tert-butyl ether molar ratio is from 3:1 to 20:1.
Claim 11
Dependent Claim 35 words
A process according to claim 1, which further comprises fractionating the methanol-containing wash stream from step (e), and separately recovering a methanol fraction and a water fraction, said methanol fraction being recycled to step (a).
Claim 12
Dependent Claim 21 words
A process according to claim 1, wherein the methanol/isobutene molar ratio of steps (a) and (b) is from 1.02:1 to 2:1.

References Cited (Backward Citations)

US3726942A Cited
US3979461A Cited
US4219678A Cited
US4144138A Cited
US4198530A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-04-12 1985-10-12 1986-04-13 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-04-12 1989-10-12 1990-04-13 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-04-12 1993-10-12 1994-04-13 $7700.00 Window Closed / Lapsed

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