GB775815A - Regeneration of solid granular contact material - Google Patents
Regeneration of solid granular contact materialInfo
- Publication number
- GB775815A GB775815A GB5170/55A GB517055A GB775815A GB 775815 A GB775815 A GB 775815A GB 5170/55 A GB5170/55 A GB 5170/55A GB 517055 A GB517055 A GB 517055A GB 775815 A GB775815 A GB 775815A
- Authority
- GB
- United Kingdom
- Prior art keywords
- bed
- air
- contact material
- regeneration
- pipes
- 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
- B01J8/08—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles
- B01J8/12—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by gravity in a downward flow
- B01J8/125—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with moving particles moved by gravity in a downward flow with multiple sections one above the other separated by distribution aids, e.g. reaction and regeneration sections
-
- 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
- B01J8/0015—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor
- B01J8/003—Feeding of the particles in the reactor; Evacuation of the particles out of the reactor in a downward flow
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
In the regeneration of spent solid granular contact material containing a carbonaceous contaminent by burning with air, the contact material gravitates downwardly as a compact bed, air is introduced into the bed at a plurality of points uniformly distributed across the bed at a level intermediate the top and bottom of the bed and at least a portion of the air flows downwardly with the contact material and is removed as flue gas from the lower portion of the bed, and the distance between adjacent points of air introduction is less than 10 inches, preferably between 5 and 10 inches. As a result of the closeness of spacing of the air inlets, the temperature differences at <PICT:0775815/III/1> different points across the bed are levelled out more rapidly as the solid descends, and thus a more even regeneration takes place and the burning capacity of the regenerator is increased. As shown in Fig. 3, solids enter at 53 and pass down pipes 55, while air enters at 51, passing down pipes 56 to outlets 57; part of the air leaves at 59 and the remainder flows upward, leaving at 58. Cooling coils may be arranged just above the bottom of the bed. A distributer for use at the bottom of the air introduction pipes 56 comprises four pipes 67, Fig. 8, and a central pipe 68 provided with an orifice plate 69. An alternative form of distributer comprises a central vertical pipe 70, Fig. 11, an orifice plate 74, and a series of vertical slots in the pipe 70 communicating with triangular ears 71. The regeneration may form part of a continuous process for the cracking or hydroforming of hydrocarbons in which contact material gravitates as a compact bed through reaction and regeneration zones and is then transferred upwardly in a stream of lift gas to the top of the reaction zone. Specification 689,369 is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US775815XA | 1954-03-11 | 1954-03-11 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB775815A true GB775815A (en) | 1957-05-29 |
Family
ID=22138922
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB5170/55A Expired GB775815A (en) | 1954-03-11 | 1955-02-21 | Regeneration of solid granular contact material |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB775815A (en) |
-
1955
- 1955-02-21 GB GB5170/55A patent/GB775815A/en not_active Expired
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US2440475A (en) | Process and apparatus for continuous catalysis | |
US2884373A (en) | Method and apparatus for heating fluids | |
US2521195A (en) | Fluidized solids conversion system | |
US2512562A (en) | Catalytic reaction apparatus | |
KR880701352A (en) | Fluidized bed reactor | |
US2542887A (en) | Apparatus for pyrolytic conversion | |
ES449170A1 (en) | Heat exchanger for fluidized bed reactor | |
US2389493A (en) | Method and apparatus for the conversion of hydrocarbons | |
US2436780A (en) | Method for handling a contact mass | |
US2499304A (en) | Method and apparatus for hydrocarbon conversion | |
US2458498A (en) | Method and apparatus for conversion of fluid hydrocarbons | |
US2458358A (en) | Process of regenerating a moving bed of solid catalyst | |
US2545165A (en) | Gas-solid contacting apparatus, including means for stripping solid particles | |
US2509014A (en) | Method and apparatus for heattreating particle form solids | |
GB1147899A (en) | A process for controlling the temperature in and improving the performance of endothermic processes carried out in a fluidised bed | |
GB775815A (en) | Regeneration of solid granular contact material | |
US2471085A (en) | Fluid catalyst process for the conversion of hydrocarbons | |
US2471034A (en) | Fluidized catalytic conversion of hydrocarbons | |
US2434202A (en) | Method and apparatus for contacting gases with particle form solid contact materials | |
US2471064A (en) | Stripping of spent catalyst in hydrocarbon conversion | |
US2448334A (en) | Pyrolytic conversion of hydrocarbons | |
US2493672A (en) | Apparatus for hydrocarbon conversion | |
US2994666A (en) | Regeneration of finely divided catalysts | |
US2467850A (en) | Apparatus for catalytic reactions | |
US2548026A (en) | Apparatus for pyrolytic conversion of hydrocarbons |