GB707281A - Method and apparatus for the removal of carbonaceous deposits from powdered solids - Google Patents
Method and apparatus for the removal of carbonaceous deposits from powdered solidsInfo
- Publication number
- GB707281A GB707281A GB22810/52A GB2281052A GB707281A GB 707281 A GB707281 A GB 707281A GB 22810/52 A GB22810/52 A GB 22810/52A GB 2281052 A GB2281052 A GB 2281052A GB 707281 A GB707281 A GB 707281A
- Authority
- GB
- United Kingdom
- Prior art keywords
- stripping
- vessel
- zone
- gas
- stripping zone
- 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
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/1845—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with particles moving upwards while fluidised
- B01J8/1854—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles with particles moving upwards while fluidised followed by a downward movement inside the reactor to form a loop
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
- B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
- B01J8/26—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with two or more fluidised beds, e.g. reactor and regeneration installations
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
The method of regenerating finely divided non- combustible solids contaminated with carbonaceous deposits as claimed in the parent Specification is modified by injecting a stripping gas into the bottom of the bed of regenerated solids forming a seal between the stripping zone and burning zone, in order to remove inert combustion gases. The apparatus used comprises a vessel 11 having a combustion gas outlet 23, a partition 12 dividing the vessel into burning and stripping zones, a second partition 13 dividing the stripping zone into two separate zones, a mixing vessel 18 in the lower stripping zone, a conduit 19 leading from the upper stripping zone to the mixing vessel a conduit 9 leading to the mixing vessel for introducing solids to be regenerated, a conduit 7 for withdrawal of regenerated solids, an outlet conduit 21 for stripping gas from the lower stripping zone, and separate means 15, 17, 24 for introducing gases into the two stripping zones and the burning zone. Vertical baffles 14, 16 are provided in the stripping zones. Back pressure control valve 22 <PICT:0707281/III/1> is regulated so that the level of the solid in the lower stripping zone is above the baffles but below the mixing vessel. Steam may be used as the stripping gas and air as the burning gas. Catalytic cracking is carried out in vessel 1, catalyst for regeneration being withdrawn from well 6. The cracking vessel comprises a tall narrow portion providing a fluidized bed having a ratio of height to diameter of at least 6, and a wider disengaging portion at the top. Stripping gas from the lower stripping zone may pass to the space above the fluidized bed in vessel 1, and from the upper stripping zone to the combustion gas outlet 23.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US680604XA | 1950-02-28 | 1950-02-28 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB707281A true GB707281A (en) | 1954-04-14 |
Family
ID=22080169
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4595/51A Expired GB680604A (en) | 1950-02-28 | 1951-02-26 | Method and apparatus for the removal of carbonaceous deposits from powdered solids |
GB22810/52A Expired GB707281A (en) | 1950-02-28 | 1952-09-11 | Method and apparatus for the removal of carbonaceous deposits from powdered solids |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB4595/51A Expired GB680604A (en) | 1950-02-28 | 1951-02-26 | Method and apparatus for the removal of carbonaceous deposits from powdered solids |
Country Status (3)
Country | Link |
---|---|
DE (1) | DE934583C (en) |
FR (1) | FR1068841A (en) |
GB (2) | GB680604A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1001441B (en) * | 1954-05-12 | 1957-01-24 | Exxon Research Engineering Co | Process for the regenerative reforming of hydrocarbons |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2401739A (en) * | 1941-08-25 | 1946-06-11 | Standard Oil Co | Cocurrent-countercurrent regenerator |
US2617708A (en) * | 1950-05-22 | 1952-11-11 | Shell Dev | Process and apparatus for contacting fluidized solids with gaseous fluids |
-
1951
- 1951-02-26 GB GB4595/51A patent/GB680604A/en not_active Expired
-
1952
- 1952-09-11 FR FR1068841D patent/FR1068841A/en not_active Expired
- 1952-09-11 GB GB22810/52A patent/GB707281A/en not_active Expired
- 1952-09-12 DE DEN6066A patent/DE934583C/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
GB680604A (en) | 1952-10-08 |
DE934583C (en) | 1955-10-27 |
FR1068841A (en) | 1954-07-01 |
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