Process for co-producing para-xylene and metaxylene, comprising two separation steps
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United States of America Patent
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Jan 4, 2005
Grant Date -
Oct 3, 2002
app pub date -
Mar 29, 2002
filing date -
Mar 29, 2001
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Abstract
A process is described for co-producing metaxylene and paraxylene from a hydrocarbon feed comprising two separation steps. The first step of the process is a counter-current simulated moving bed system in a chromatographic column containing at least five zones, comprising injecting the feed and injecting a desorbent and delivering an extract, a raffinate and an intermediate raffinate either continuously or discontinuously. The extract is distilled to obtain a paraxylene with a purity of at least 99.7%. The raffinate, which is richer in metaxylene, is distilled to extract the desorbent and injected into a counter-current simulated moving bed continuously delivering an extract and a raffinate. One of these two streams is enriched in metaxylene. The most metaxylene-rich stream is distilled to obtain metaxylene with a purity of more than 99%.
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- 15 United States
- 10 France
- 8 Japan
- 7 China
- 5 Korea
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Patent Owner(s)
- INSTITUT FRANCAIS DU PETROLE
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Inventor(s)
Inventor Name | Address | # of filed Patents | Total Citations |
---|---|---|---|
Hotier, Gerard | Rueil Malmaison, FR | 69 | 820 |
Leflaive, Philibert | Sceaux, FR | 82 | 292 |
Methivier, Alain | Orleans, FR | 19 | 201 |
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Surcharge after expiration - Late payment is unavoidable | $700.00 | $350.00 | $175.00 |
Surcharge after expiration - Late payment is unintentional | $1,640.00 | $820.00 | $410.00 |
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