IE34000B1 - Furnace oils from waxy gas oils - Google Patents
Furnace oils from waxy gas oilsInfo
- Publication number
- IE34000B1 IE34000B1 IE51/70A IE5170A IE34000B1 IE 34000 B1 IE34000 B1 IE 34000B1 IE 51/70 A IE51/70 A IE 51/70A IE 5170 A IE5170 A IE 5170A IE 34000 B1 IE34000 B1 IE 34000B1
- Authority
- IE
- Ireland
- Prior art keywords
- gas oil
- catalytic cracking
- catalyst
- end point
- boiling point
- Prior art date
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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
Abstract
1,253,762. Cracking hydrocarbons. TEXACO DEVELOPMENT CORP. 29 Dec., 1969 [15 Jan., 1969], No. 63054/69. Heading C5E. A process for preparing furnace oil from waxy gas oil comprises: (a) subjecting a waxy gas oil fraction to catalytic cracking under conditions effecting conversion of not less than 30 vol. per cent based on fresh feed, (b) separating from the catalytic cracking effluent a light gas oil having a pour point of 0 F. or lower, (c) separating from the catalytic cracking effluent an intermediate gas oil having an inital boiling point corresponding to the end point of the light gas oil of step (b) and an end point in the range of 650 to 750 F., (d) separating from the catalytic cracking effluent a heavy gas oil fraction having an initial boiling point corresponding to the end point of the intermediate gas oil of step (c), and, (e) passing said intermediate gas oil to said catalytic cracking zone as part of the feed thereto. The light gas oil fraction may have a boiling range of 430-550 F. and a pour point of about 0 F. and the intermediate gas oil fraction may have an initial boiling point of about 550 F. and an end point in the range of 650 to 750 F. In this process the initial boiling point, IBP, of the feed to the catalytic cracking unit is usually above 400 F. The cracking catalyst may comprise a molecular sieve or crystalline alumino-silicate base carrying catalytic metal additives for example cerium or lanthanum or their oxides or sulphides, a natural clay catalyst comprising silica-alumina, a synthetic silica-alumina catalyst or a silicamagnesia catalyst.
[GB1253762A]
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US79364369A | 1969-01-15 | 1969-01-15 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| IE34000L IE34000L (en) | 1970-07-15 |
| IE34000B1 true IE34000B1 (en) | 1975-01-08 |
Family
ID=25160440
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| IE51/70A IE34000B1 (en) | 1969-01-15 | 1970-01-14 | Furnace oils from waxy gas oils |
Country Status (13)
| Country | Link |
|---|---|
| BE (1) | BE744374A (en) |
| BR (1) | BR7015920D0 (en) |
| CA (1) | CA948581A (en) |
| DE (1) | DE1964799C3 (en) |
| DK (1) | DK132587C (en) |
| ES (1) | ES375430A1 (en) |
| FI (1) | FI53980C (en) |
| FR (1) | FR2028392B1 (en) |
| GB (1) | GB1253762A (en) |
| IE (1) | IE34000B1 (en) |
| NL (1) | NL152922B (en) |
| SE (1) | SE362656B (en) |
| ZA (1) | ZA698873B (en) |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2641573A (en) * | 1950-11-30 | 1953-06-09 | Standard Oil Dev Co | Production of motor fuels from petroleum oils |
| US2925376A (en) * | 1956-02-13 | 1960-02-16 | Sun Oil Co | Hydrocarbon conversion |
| US2918423A (en) * | 1957-01-14 | 1959-12-22 | Sun Oil Co | Hydrocarbon conversion process |
-
1969
- 1969-12-22 ZA ZA698873*A patent/ZA698873B/en unknown
- 1969-12-24 DE DE1964799A patent/DE1964799C3/en not_active Expired
- 1969-12-29 GB GB63054/69A patent/GB1253762A/en not_active Expired
-
1970
- 1970-01-09 BR BR215920/70A patent/BR7015920D0/en unknown
- 1970-01-13 BE BE744374D patent/BE744374A/en unknown
- 1970-01-14 SE SE00424/70A patent/SE362656B/xx unknown
- 1970-01-14 ES ES375430A patent/ES375430A1/en not_active Expired
- 1970-01-14 IE IE51/70A patent/IE34000B1/en unknown
- 1970-01-15 CA CA072,241A patent/CA948581A/en not_active Expired
- 1970-01-15 FR FR7001359A patent/FR2028392B1/fr not_active Expired
- 1970-01-15 NL NL707000608A patent/NL152922B/en unknown
- 1970-01-15 FI FI112/70A patent/FI53980C/en active
- 1970-01-15 DK DK16370*#A patent/DK132587C/en active
Also Published As
| Publication number | Publication date |
|---|---|
| FR2028392B1 (en) | 1974-03-15 |
| ES375430A1 (en) | 1972-05-01 |
| IE34000L (en) | 1970-07-15 |
| DK132587C (en) | 1976-05-31 |
| FR2028392A1 (en) | 1970-10-09 |
| BR7015920D0 (en) | 1973-01-23 |
| DE1964799B2 (en) | 1973-02-01 |
| FI53980B (en) | 1978-05-31 |
| NL152922B (en) | 1977-04-15 |
| FI53980C (en) | 1978-09-11 |
| DK132587B (en) | 1976-01-05 |
| SE362656B (en) | 1973-12-17 |
| GB1253762A (en) | 1971-11-17 |
| DE1964799C3 (en) | 1973-09-13 |
| NL7000608A (en) | 1970-07-17 |
| CA948581A (en) | 1974-06-04 |
| DE1964799A1 (en) | 1970-07-16 |
| BE744374A (en) | 1970-07-13 |
| ZA698873B (en) | 1971-04-28 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4911823A (en) | Catalytic cracking of paraffinic feedstocks with zeolite beta | |
| GB1417525A (en) | Method for converting hydrocarbons by cracking in the presence of a zeolite cracking catalyst | |
| US3303123A (en) | Catalytic cracking of residuum oils containing metal contaminants in several stages | |
| GB1349911A (en) | Catalytic cracking of naphtha and gas oil | |
| GB1499682A (en) | Catalyst regeneration process | |
| DE69126638D1 (en) | Refining sludge heavy oil fractions | |
| ES8107294A1 (en) | Carbo-metallic oil conversion with liquid water | |
| GB923246A (en) | Conversion of residual oil to gasoline | |
| ES8107293A1 (en) | High metal carbo-metallic oil conversion | |
| KR890008301A (en) | Process for preparing light hydrocarbon distillates by hydrocracking and catalysis | |
| GB1144885A (en) | Hydrocarbon conversion catalyst | |
| AU570253B2 (en) | Carbo-metallic oil conversion | |
| CA1132075A (en) | Staged process for the production of middle distillate from a heavy distillate | |
| US3689402A (en) | Furnace oil from waxy gas oils | |
| IE34000L (en) | Cracking waxy gas oils | |
| GB1381004A (en) | Preparation of high viscosity index lubricating oils | |
| ES368707A1 (en) | Hydrocracking process | |
| GB1191958A (en) | Three-Stage Hydrocracking Process | |
| GB1193220A (en) | A process for the preparation of Base Oils for the Production of Lubricating Oil | |
| GB1314879A (en) | Production of lubricating oils | |
| US3575844A (en) | Hydrocracking process | |
| US3152980A (en) | Hydrocracking with reduced catalyst aging | |
| GB1250548A (en) | ||
| ES8505400A1 (en) | A process for the production of low-asphaltenes hydrocarbon mixtures. | |
| US3909391A (en) | Recovery of aluminum chloride/palladium chloride hydrocracking catalyst mixture |