GB1306160A - - Google Patents
Info
- Publication number
- GB1306160A GB1306160A GB1306160DA GB1306160A GB 1306160 A GB1306160 A GB 1306160A GB 1306160D A GB1306160D A GB 1306160DA GB 1306160 A GB1306160 A GB 1306160A
- Authority
- GB
- United Kingdom
- Prior art keywords
- liquid
- separated
- range
- hydrocarbons
- recombining
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G47/00—Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions
Abstract
1306160 Making combustible gas; reforming naphtha UNIVERSAL OIL PRODUCTS CO 6 July 1970 32618/70 Heading C5E A method for converting hydrocarbons 10, e.g. naphthas boiling in the range 32‹ to 232‹ C., to produce H 2 at 26, gaseous hydrocarbons at 35, and light liquid hydrocarbons at 30, 34, comprises reforming the feed at 11 at relatively low pressure, i.e. in the range 50 to 1200 p.s.i.g.; separating the effluent at 14 into a first liquid phase 16 and a first H 2 -containing phase 15; increasing the pressure of both phases to a relatively high value (which is preferably at least 50 p.s.i. more than the low pressure), and recombining the phases. An H 2 -containing stream 22 is separated at 21, a portion 12 being recycled, and the remainder being cooled at 24 and a condensate 27 separated at 25 for recombining with the liquid 23 from the separator 21. This liquid is fractionated, condensed and separated to provide the required fractions. The stage 11 uses a fixed bed Pt catalyst, and is preferably operated at pressures in the range 85 to 200 p.s.i.g.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB3261870 | 1970-07-06 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB1306160A true GB1306160A (en) | 1973-02-07 |
Family
ID=10341421
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB1306160D Expired GB1306160A (en) | 1970-07-06 | 1970-07-06 |
Country Status (1)
| Country | Link |
|---|---|
| GB (1) | GB1306160A (en) |
-
1970
- 1970-07-06 GB GB1306160D patent/GB1306160A/en not_active Expired
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PS | Patent sealed | ||
| PCNP | Patent ceased through non-payment of renewal fee |