HUP9903099A2 - Process for the gasolines production - Google Patents
Process for the gasolines productionInfo
- Publication number
- HUP9903099A2 HUP9903099A2 HU9903099A HUP9903099A HUP9903099A2 HU P9903099 A2 HUP9903099 A2 HU P9903099A2 HU 9903099 A HU9903099 A HU 9903099A HU P9903099 A HUP9903099 A HU P9903099A HU P9903099 A2 HUP9903099 A2 HU P9903099A2
- Authority
- HU
- Hungary
- Prior art keywords
- fraction
- sent
- naphtha fraction
- production
- heavy naphtha
- Prior art date
Links
- 238000004519 manufacturing process Methods 0.000 title abstract 2
- 238000000034 method Methods 0.000 title abstract 2
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 abstract 3
- 229930195733 hydrocarbon Natural products 0.000 abstract 2
- 150000002430 hydrocarbons Chemical class 0.000 abstract 2
- 230000003197 catalytic effect Effects 0.000 abstract 1
- 239000010779 crude oil Substances 0.000 abstract 1
- 238000004821 distillation Methods 0.000 abstract 1
- 238000006317 isomerization reaction Methods 0.000 abstract 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 abstract 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Abstract
High yield process for the production of high octane and low benzene content gasolines involves a cycle where a crude oil is fed into an atmospheric distillation unit from which a virgin naphtha fraction is obtained, which in turn is sent to a splitting unit to produce a light tops fraction and heavy naphtha fraction. The light tops fraction is sent to an isomerisation unit and the heavy naphtha fraction is sent to a catalytic reformer. The heavy naphtha fraction contains no more than 0.5 vol.% 6C hydrocarbons and the light tops fraction contains no more than 4 vol.% 7 C+ hydrocarbons.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| HU9903099A HUP9903099A3 (en) | 1997-07-21 | 1997-07-21 | Process for the gasolines production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| HU9903099A HUP9903099A3 (en) | 1997-07-21 | 1997-07-21 | Process for the gasolines production |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| HUP9903099A2 true HUP9903099A2 (en) | 1999-12-28 |
| HUP9903099A3 HUP9903099A3 (en) | 2000-07-28 |
Family
ID=89999313
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| HU9903099A HUP9903099A3 (en) | 1997-07-21 | 1997-07-21 | Process for the gasolines production |
Country Status (1)
| Country | Link |
|---|---|
| HU (1) | HUP9903099A3 (en) |
-
1997
- 1997-07-21 HU HU9903099A patent/HUP9903099A3/en unknown
Also Published As
| Publication number | Publication date |
|---|---|
| HUP9903099A3 (en) | 2000-07-28 |
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