Use of divided wall technology to produce high purity methanol

US12180129B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-12180129-B2
Application numberUS-201917275015-A
CountryUS
Kind codeB2
Filing dateSep 11, 2019
Priority dateSep 12, 2018
Publication dateDec 31, 2024
Grant dateDec 31, 2024

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

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Methods and systems for producing high purity methanol and isobutene from crude MTBE feed using multiple divided wall columns are provided. The methods can include purifying the MTBE, dissociating the MTBE to produce isobutene and methanol, purifying the isobutene and recovering/purifying methanol.

First claim

Opening claim text (preview).

What is claimed is: 1. A process for the coproduction of isobutene and high purity methanol, the process comprising: a. separating a feed stream comprising crude methyl tertiary butyl ether (MTBE) in a first fractionation system to recover an MTBE product stream comprising at least 94 wt % MTBE, and to recover a heavies stream; b. contacting the MTBE product stream with a catalyst to provide an effluent comprising isobutene and methanol; c. contacting the effluent comprising isobutene and methanol with one or more extractants to produce an extractant/methanol stream and a mixed isobutene stream; d. feeding the mixed isobutene stream into a second fractionation system to recover a stream comprising isobutene comprising at least 95 wt % isobutene; e. feeding the extractant/methanol stream into a third fractionation system comprising a divided wall distillation column to recover a lights fraction, a methanol product stream comprising at least 95 wt % methanol and a heavies fraction comprising the extractant; and recycling at least a portion of the lights fraction from the third fractionation system to the first fractionation system. 2. The process of claim 1 , wherein the feed stream comprises crude MTBE provided from an etherification reaction zone and a supplemental MTBE feed stream. 3. The process of claim 2 , further comprising feeding the lights fraction from the third fractionation system to the etherification reaction zone. 4. The process of claim 1 , wherein the feed stream further comprises diisobutene (DIB), tertiary butyl alcohol (TBA) and 2-methoxybutane (MSBE). 5. The process of claim 1 , wherein the extractant comprises water. 6. The process of claim 1 , wherein the first, second, and third fractionation systems each comprise a divided wall distillation column. 7. The process of claim 1 , further comprising removing a stream comprising MTBE/isobutene from the second fractionation system. 8. The process of claim 7 , further comprising recycling the MTBE/isobutene to the first fractionation system. 9. The process of claim 1 , wherein the methanol stream comprises at least 99.8 wt % methanol. 10. A process for the coproduction of isobutene and high purity methanol, the process comprising: a. separating a feed stream comprising crude methyl tertiary butyl ether (MTBE) in a first fractionation system to recover an MTBE product stream comprising at least 94 wt % MTBE, and to recover a heavies stream; b. contacting the MTBE product stream with a catalyst to provide an effluent comprising isobutene and methanol; c. contacting the effluent with one or more extractants to produce an extractant/methanol stream and a mixed isobutene stream; d. feeding the mixed isobutene stream into a second fractionation system to recover a stream comprising isobutene and comprising at least 95 wt % isobutene; e. feeding the extractant/methanol stream into a third fractionation system comprising a divided wall distillation column to recover an overheads fraction, a methanol side draw product stream comprising at least 95 wt % methanol and a bottoms stream comprising the extractant. 11. The process of claim 10 , further comprising removing a stream comprising MTBE/isobutene from the second fractionation system. 12. The process of claim 11 , further comprising recycling the MTBE/isobutene to the first fractionation system. 13. The process of claim 10 , further comprising recycling at least a portion of the lights fraction from the third fractionation system to the first fractionation column. 14. A process for the coproduction of isobutene and high purity methanol, the process comprising: a. separating a feed stream comprising crude methyl tertiary butyl ether (MTBE), diisobutene (DIB), tertiary butyl alcohol (TBA) and 2-methoxybutane (MSBE) in a first fractionation system to recover an MTBE product stream comprising at least 94 wt % MTBE, and to recover a heavies stream comprising a mixture of MTBE, tert-butyl alcohol (TBA), and 2-methoxybutane (MSBE); b. contacting the MTBE product stream with a catalyst to provide an effluent comprising isobutene, methanol, and residual MTBE; c. contacting the effluent with one or more extractants to produce an extractant/methanol stream and a mixed isobutene/MTBE stream; d. feeding the mixed isobutene/MTBE stream into a second fractionation system to recover a stream comprising isobutene comprising at least 94 wt % isobutene and a heavies stream comprising MTBE/isobutene; e. recycling the heavies stream comprising MTBE/isobutene to the first fractionation system; f. feeding the extractant/methanol stream into a third fractionation system comprising a divided wall distillation column to recover an overheads fraction, a methanol side draw product stream comprising at least 95 wt % methanol and a bottoms stream comprising residual MTBE, methanol, and the extractant; and g. recycling the bottoms stream comprising residual MTBE, methanol, and the extractant to the first fractionation system.

Assignees

Inventors

Classifications

  • Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring · CPC title

  • by extractive distillation · CPC title

  • by extractive distillation · CPC title

  • C07C1/20Primary

    starting from organic compounds containing only oxygen atoms as heteroatoms · CPC title

  • by distillation · CPC title

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What does patent US12180129B2 cover?
Methods and systems for producing high purity methanol and isobutene from crude MTBE feed using multiple divided wall columns are provided. The methods can include purifying the MTBE, dissociating the MTBE to produce isobutene and methanol, purifying the isobutene and recovering/purifying methanol.
Who is the assignee on this patent?
Lummus Technology Inc
What technology area does this patent fall under?
Primary CPC classification C07C1/20. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Dec 31 2024 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 1 related publication on this page (citations in our corpus or others sharing the same primary CPC).