US4816607A
Expired / Lapsed
US
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Integrated etherification process with recycle post treatment
Assignee: Honeywell UOP LLC
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Filing: 1988-06-24
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Granted: 1989-03-28
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Expires: 2008-06-24
Abstract
Abstract A multistep hydrocarbon conversion process for the production of ethers including methyl tertiary butyl ether (MTBE) from light paraffins and alcohols is disclosed. A mixture of C 4 isoparaffins, normal paraffins, an etherification recycle and butane isomerization effluent enter a deisobutanizer column. Normal paraffins withdrawn from the fractionator are isomerized and returned to the fractionator, and isoparaffins are withdrawn from the fractionator and dehydrogenated. The resulting olefins enter an etherification zone for reaction of isobutene with a C 2 -C 5 alcohol. Unreacted paraffins and olefins comprise a portion of the etherification effluent entering the deisobutanizer. After separation for recovery of the ether product, unreacted paraffins and olefins are passed through a dehydrogenation zone for saturation of the olefins and then returned to the deisobutanizer column. Normal butanes are withdrawn as a sidecut from the deisobutanizer. The sidecut passes to an isomerization zone and a mixture of isobutane and normal butane is recycled to the deisobutanizer. In a highly preferred embodiment, spent catalyst from the isomerization zone fulfills the catalyst requirement of the dehydrogenation zone.
Inventors
- 👤 Bipin V. Vora
- 👤 Peter R. Pujado
- 👤 Richard E. Conser
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-25 09:42
CPC Classifications
C; C07; C07C; C07C41/00; C07C41/01; C07C41/05; C07C41/06; C07C5/00; C07C5/22; C07C5/27; C07C5/2767; C07C5/277; C07C5/2791
Claims Analysis
Total Claims: 13
Claim 1
Independent Claim
196 words
A hydrocarbon conversion process which comprises the steps of: (a) passing a feed stream which comprises C 4 -C 6 paraffins to a fractionation section; (b) recovering a first stream rich in isoparaffin from the fractionation section; (c) passing said first stream to a dehydrogenation unit and recovering a second stream rich in the isoolefin corresponding to the isoparaffin in said first stream and hydrogen containing gas; (d) passing at least a portion of said isoolefin from said second stream and a C 1 -C 5 alcohol to an etherification zone and recovering a third stream; (e) separating said third stream to recover an ether rich product stream and an olefin containing fourth stream; (f) passing said fourth stream to a hydrogenation zone to saturate said olefins and recovering a fifth stream comprising saturated hydrocarbons; (g) returning said fifth stream to said fractionation section; (h) recovering a sixth stream from said fractionation section, said sixth stream being rich in normal paraffins; (i) passing said sixth stream to an isomerization zone and recovering a seventh stream comprising corresponding isoparaffins and normal paraffins; and (j) returning at least a portion of said seventh stream to said fractionation section.
Claim 2
Dependent Claim
196 words
A hydrocarbon conversion process which comprises the steps of: (a) passing a feed stream which comprises C 4 -C 6 paraffins to a fractionation section; (b) recovering a first stream rich in isoparaffin from the fractionation section; (c) passing said first stream to a dehydrogenation unit and recovering a second stream rich in the isoolefin corresponding to the isoparaffin in said first stream and hydrogen containing gas; (d) passing at least a portion of said isoolefin from said second stream and a C 1 -C 5 alcohol to an etherification zone and recovering a third stream; (e) separating said third stream to recover an ether rich product stream and an olefin containing fourth stream; (f) passing said fourth stream to a hydrogenation zone to saturate said olefins and recovering a fifth stream comprising saturated hydrocarbons; (g) returning said fifth stream to said fractionation section; (h) recovering a sixth stream from said fractionation section, said sixth stream being rich in normal paraffins; (i) passing said sixth stream to an isomerization zone and recovering a seventh stream comprising corresponding isoparaffins and normal paraffins; and (j) returning at least a portion of said seventh stream to said fractionation section.
Claim 3
Dependent Claim
27 words
The process of claim 1 further characterized in that said second stream passes through a separator to remove light gases prior to passing to said etherification zone.
Claim 4
Dependent Claim
27 words
The process of claim 2 further characterized in that at least a portion of the hydrogen containing gas from said second stream passes to said hydrogenation zone.
Claim 5
Dependent Claim
14 words
The process of claim 1 further characterized in that said feed comprises mixed butanes.
Claim 6
Dependent Claim
53 words
The process of claim 1 further characterized in that said isomerization zone uses a catalyst that retains a dehydrogenation function after substantial deactivation of its isomerization function, and at least a portion of said catalyst is used to fulfill the catalyst requirements of said hydrogenation zone after it has undergone substantial isomerization deactivation.
Claim 7
Dependent Claim
30 words
The process of claim 5 further characterized in that said catalyst comprises a platinum group metal in a weight ratio of 0.05 to 1 wt. % on an alumina support.
Claim 8
Dependent Claim
36 words
The process of claim 1 wherein said fractionation section comprises a single column and said first stream comprises a net overhead stream from said column and said sixth stream comprises an intermediate stream from said column.
Claim 9
Dependent Claim
211 words
A hydrocarbon conversion for producing methyl tertiary butyl ether from feed materials comprising mixed butanes and butenes, and a methyl alcohol, said process comprising: (a) passing said feed stream of said mixed butanes and butenes to a fractionation column; (b) recovering an overhead stream consisting essentially of isobutane; (c) passing said overhead stream to a dehydrogenation zone to convert isobutane to isobutene, and recovering a first effluent stream rich in isobutene; (d) passing at least a portion of said first effluent and an input stream of methanol to an etherification zone and separating the effluent from said etherification zone to recover an MTBE rich product stream, and a first recycle stream comprising isobutane and olefins; (e) passing said first recycle stream to a hydrogenation zone to saturate said olefins and recovering a second recycl stream, said second recycle stream being substantially free of olefins; (f) passing said first recycle stream to said column; (g) withdrawing a higher boiling fraction from said column, said higher boiling fraction being rich in normal butene; and (h) passing said higher boiling fraction to an isomerization zone to convert normal butane to isobutane and recovering a second effluent stream, rich in isobutane, and recycling at least a portion of said second effluent stream to said column.
Claim 10
Dependent Claim
211 words
A hydrocarbon conversion for producing methyl tertiary butyl ether from feed materials comprising mixed butanes and butenes, and a methyl alcohol, said process comprising: (a) passing said feed stream of said mixed butanes and butenes to a fractionation column; (b) recovering an overhead stream consisting essentially of isobutane; (c) passing said overhead stream to a dehydrogenation zone to convert isobutane to isobutene, and recovering a first effluent stream rich in isobutene; (d) passing at least a portion of said first effluent and an input stream of methanol to an etherification zone and separating the effluent from said etherification zone to recover an MTBE rich product stream, and a first recycle stream comprising isobutane and olefins; (e) passing said first recycle stream to a hydrogenation zone to saturate said olefins and recovering a second recycl stream, said second recycle stream being substantially free of olefins; (f) passing said first recycle stream to said column; (g) withdrawing a higher boiling fraction from said column, said higher boiling fraction being rich in normal butene; and (h) passing said higher boiling fraction to an isomerization zone to convert normal butane to isobutane and recovering a second effluent stream, rich in isobutane, and recycling at least a portion of said second effluent stream to said column.
Claim 11
Dependent Claim
40 words
The process of claim 8 further characterized in that said first effluent stream is separated to recover a hydrogen rich gas stream and at least a portion of said gas stream is passed to said hydrogenation zone to supply hydrogen.
Claim 12
Dependent Claim
53 words
The process of claim 8 further characterized in that said isomerization zone uses a catalyst that retains a dehydrogenation function after substantial deactivation of its isomerization function, and at least a portion of said catalyst is used to fulfill the catalyst requirements of said hydrogenation zone after it has undergone substantial isomerization deactivation.
Claim 13
Dependent Claim
29 words
The process of claim 10 further characterized in that said catalyst comprises a platinum group metal in weight ratio of 0.05 to 1 wt. % on an alumina support.
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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) | 1992-03-27 | 1992-09-26 | 1993-03-28 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1996-03-27 | 1996-09-26 | 1997-03-28 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 2000-03-27 | 2000-09-26 | 2001-03-28 | $7700.00 | Window Closed / Lapsed |