US2003141221A1PendingUtilityA1
Upgrading Fischer-Tropsch and petroleum-derived naphthas and distillates
Priority: Jan 31, 2002Filed: Jan 31, 2002Published: Jul 31, 2003
Est. expiryJan 31, 2022(expired)· nominal 20-yr term from priority
C10G 2/32C10G 2400/02
39
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Claims
Abstract
A process for upgrading at least one of a Fischer-Tropsch naphtha and a Fischer-Tropsch distillate to produce at least one of a gasoline component, a distillate fuel or a lube base feedstock component. The process includes reforming a Fischer-Tropsch naphtha to produce hydrogen by-product and a gasoline component with a research octane rating of at least about 80. The process further includes upgrading a Fischer-Tropsch distillate using the hydrogen by-product to produce a distillate fuel and/or a lube base feedstock component.
Claims
exact text as granted — not AI-modifiedWhat is claimed is:
1 . A process for upgrading a Fischer-Tropsch naphtha to produce a gasoline component, the process comprising:
a) hydrotreating a Fischer-Tropsch naphtha to remove oxygenates producing hydrotreated Fischer-Tropsch naphtha; b) reforming said hydrotreated Fischer-Tropsch naphtha producing hydrogen by-product and a gasoline component having a research octane rating of at least about 80; and c) recirculating said hydrogen by-product to hydrotreat said Fischer-Tropsch naphtha.
2 . The process of claim 1 , further comprising hydrotreating said Fischer-Tropsch naphtha using a catalyst comprising at least one of a noble metal and a non-noble metal.
3 . The process of claim 2 , wherein said catalyst comprises a noble metal selected from the group consisting essentially of Pd, Pt, and combinations thereof.
4 . The process of claim 2 , wherein said catalyst comprises a non-noble metal that is sulfided in form.
5 . The process of claim 2 , wherein said non-noble metal is sulfided with dimethyldisulfide.
6 . The process of claim 2 , wherein said non-noble metal is selected from the group consisting essentially of Ni, Co, W, Mo and combinations thereof.
7 . The process of claim 1 , wherein said gasoline component has a research octane rating of at least about 90.
8 . The process of claim 1 , wherein said gasoline component comprises at least about 10% aromatics.
9 . The process of claim 1 , wherein immediately prior to hydrotreatment, said Fischer-Tropsch naphtha comprises at least about 1 ppm sulfur.
10 . The process of claim 9 , wherein said Fischer-Tropsch naphtha comprises at least about 10 ppm sulfur.
11 . The process of claim 1 , wherein prior to hydrotreatment said Fischer-Tropsch naphtha is mixed with a petroleum-derived naphtha to obtain a blended naphtha having a sulfur level of at least about 1 ppm.
12 . The process of claim 11 , wherein said blended naphtha has a sulfur level of at least about 10 ppm.
13 . A gasoline component having a research octane rating of at least about 80 produced by the process of claim 1 .
14 . The process of claim 1 , further comprising providing additional hydrogen to supplement the hydrogen by-product obtained from said naphtha reformation for hydrotreating said Fischer-Tropsch naphtha.
15 . A process for upgrading a Fischer-Tropsch naphtha to produce a gasoline component, the process comprising:
a) hydrotreating a Fischer-Tropsch naphtha, using a catalyst comprising at least one of a noble metal and a non-noble metal, producing hydrogen by-product and a gasoline component having a research octane rating of at least about 90 and comprising at least about 10% aromatics; and b) recirculating said hydrogen by-product to hydrotreat said Fischer-Tropsch naphtha.
16 . The process of claim 15 , wherein immediately prior to hydrotreatment, said Fischer-Tropsch naphtha comprises at least about 1 ppm sulfur.
17 . A gasoline component having a research octane rating of at least about 90 produced by the process of claim 15 .
18 . A process for upgrading a Fischer-Tropsch naphtha to produce a gasoline component, the process comprising:
a) hydrotreating a Fischer-Tropsch naphtha to remove oxygenates producing hydrotreated Fischer-Tropsch naphtha; b) reforming said hydrotreated Fischer-Tropsch naphtha producing hydrogen by-product and a gasoline component having a research octane rating of at least about 80; and c) recirculating said hydrogen by-product to hydrotreat said Fischer-Tropsch naphtha; d) wherein said Fischer-Tropsch naphtha is a blended naphtha, having a sulfur level of at least about 1 ppm, obtained by mixing said Fischer-Tropsch naphtha with a petroleum-derived naphtha.
19 . The process of claim 18 , wherein said blended naphtha has a sulfur level of at least about 10 ppm.
20 . A gasoline component having an octane rating of at least about 80 produced by the process of claim 18.Join the waitlist — get patent alerts
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