GB786358A - Processes for the catalytic cracking of hydrocarbon oils - Google Patents
Processes for the catalytic cracking of hydrocarbon oilsInfo
- Publication number
- GB786358A GB786358A GB17120/55A GB1712055A GB786358A GB 786358 A GB786358 A GB 786358A GB 17120/55 A GB17120/55 A GB 17120/55A GB 1712055 A GB1712055 A GB 1712055A GB 786358 A GB786358 A GB 786358A
- Authority
- GB
- United Kingdom
- Prior art keywords
- zone
- catalyst
- passed
- line
- cracking
- 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
- C10G11/00—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
- C10G11/14—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts
- C10G11/18—Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils with preheated moving solid catalysts according to the "fluidised-bed" technique
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/20—Regeneration or reactivation
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Materials Engineering (AREA)
- General Chemical & Material Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Catalysts (AREA)
Abstract
In a two-stage process of cracking a hydrocarbon oil with finely-divided catalyst wherein a fraction, boiling above the gasoline range, of the hydrocarbon products from the 1st cracking zone is cracked in the 2nd cracking zone which is maintained at a lower temperature than the 1st zone, hot freshly-regenerated catalyst is supplied to the 1st zone, the catalyst is separted from the hydrocarbon products formed in the <FORM:0786358/III/1> 1st zone, at least 20 per cent of this once-used catalyst is passed directly to a stripping zone, the remaining part of the once-used catalyst is employed as catalyst in the 2nd cracking zone, the twice-used catalyst separated from the products of 2nd zone is passed to the aforementioned stripping zone, and the stripped catalyst is passed to the regenerator. The process affords efficient stripping of the spent catalyst. A distillate of B.R. 218-538 DEG C. obtained by vacuum-flashing a straight-run residue is passed through line 1 into cracking zone A wherein it is contacted with hot freshlyregenerated silica-alumina catalyst at about 1120 DEG F. supplied through line 18, the catalyst/oil ratio being 12. A temperature of 1020 DEG F. and a pressure of 2.5 atm. are maintained in zone A, and a conversion of 48 per cent is obtained. The total vapour products, free from catalyst, are passed to fractionator 3, and gasoline (+ gas) is separated overhead. The higher boiling oil removed from the base of the fractionator is passed to cracking zone B wherein it is contactd with about 59 per cent by weight of the catalyst withdrawn from zone A via line 6. A temperature of 910 DEG F. and a pressure of 2.2 atm. are maintained in zone B; and a conversion of 28 per cent (based on the fresh feed to the plant) is obtained therein. The total product vapours from zone B are passed to fractionator 8, from which gasoline (+ gas) is taken-off overhead while catalytically-cracked gas oil is withdrawn from the base. This gas oil may be recycled to either zone A or zone B. The spent catalyst from zone B is passed by line 11 to stripping zone C; and the remaining part of the once-used catalyst from zone A is also passed to zone C via line 14. Steam is introduced into zone C through line 12; and a temperature of 955 DEG F. is maintained therein. The hydrocarbons stripped off the mixed catalyst are withdrawn through line 13. The stripped catalyst is regenerated in zone D, air being supplied through line 16; and the regenerated catalyst is then recycled to cracking zone A by line 18. Specification 784,546 is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US786358XA | 1954-06-16 | 1954-06-16 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB786358A true GB786358A (en) | 1957-11-13 |
Family
ID=22145312
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB17120/55A Expired GB786358A (en) | 1954-06-16 | 1955-06-14 | Processes for the catalytic cracking of hydrocarbon oils |
Country Status (4)
Country | Link |
---|---|
DE (1) | DE1014691B (en) |
FR (1) | FR1132549A (en) |
GB (1) | GB786358A (en) |
NL (2) | NL198013A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0142275A2 (en) * | 1983-10-19 | 1985-05-22 | Mobil Oil Corporation | Fluidized catalytic cracking process with long residence time stripper |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2488032A (en) * | 1941-05-10 | 1949-11-15 | Standard Oil Co | Catalytic conversion of hydrocarbons and apparatus therefor |
GB571143A (en) * | 1941-10-27 | 1945-08-09 | Universal Oil Prod Co | Process for continuously contacting powdered solid material with fluids |
US2477042A (en) * | 1943-03-10 | 1949-07-26 | Standard Oil Dev Co | Method of heat exchange in fluidized hydrocarbon conversion systems |
US2460404A (en) * | 1943-09-30 | 1949-02-01 | Universal Oil Prod Co | Catalytic conversion of hydrocarbons |
US2507523A (en) * | 1946-08-31 | 1950-05-16 | Houdry Process Corp | Conversion of hydrocarbons |
US2560511A (en) * | 1947-08-09 | 1951-07-10 | Anglo Iranian Oil Co Ltd | Catalytic cracking of heavy hydrocarbons in two stages |
-
0
- NL NL102343D patent/NL102343C/xx active
- NL NL198013D patent/NL198013A/xx unknown
-
1955
- 1955-06-14 GB GB17120/55A patent/GB786358A/en not_active Expired
- 1955-06-14 FR FR1132549D patent/FR1132549A/en not_active Expired
- 1955-06-14 DE DEN10795A patent/DE1014691B/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0142275A2 (en) * | 1983-10-19 | 1985-05-22 | Mobil Oil Corporation | Fluidized catalytic cracking process with long residence time stripper |
EP0142275A3 (en) * | 1983-10-19 | 1986-06-25 | Mobil Oil Corporation | Fluidized catalytic cracking process with long residence time stripper |
Also Published As
Publication number | Publication date |
---|---|
NL102343C (en) | 1962-04-16 |
DE1014691B (en) | 1957-08-29 |
FR1132549A (en) | 1957-03-12 |
NL198013A (en) |
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