GB580621A - Regeneration of spent catalysts - Google Patents
Regeneration of spent catalystsInfo
- Publication number
- GB580621A GB580621A GB13186/44A GB1318644A GB580621A GB 580621 A GB580621 A GB 580621A GB 13186/44 A GB13186/44 A GB 13186/44A GB 1318644 A GB1318644 A GB 1318644A GB 580621 A GB580621 A GB 580621A
- Authority
- GB
- United Kingdom
- Prior art keywords
- regeneration
- regenerating gas
- reactor
- suspension
- pipe
- 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
- C10G11/182—Regeneration
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
<PICT:0580621/III/1> Catalysts contaminated with carbonaceous deposits are regenerated in two stages, first in suspension in a portion of the regenerating gas, and secondly, after separation from the combustion products, in a fluidized state with a second portion of regenerating gas. As shown in the figure, catalyst is drawn off from the bottom of reactor 1, and carried in suspension in regenerating gas through a conduit 2 into a second stage regenerator 3 in which it is fluidized by gas admitted from pipe 15. Regenerated catalyst is withdrawn at 5, mixed in pipe 4 with reactants and returned to the reactor 1.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US580621XA | 1943-05-31 | 1943-05-31 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB580621A true GB580621A (en) | 1946-09-13 |
Family
ID=22014420
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB13186/44A Expired GB580621A (en) | 1943-05-31 | 1944-07-10 | Regeneration of spent catalysts |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB580621A (en) |
-
1944
- 1944-07-10 GB GB13186/44A patent/GB580621A/en not_active Expired
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