GB578793A - Improvements relating to the conversion of fluid reactants in the presence of subdivided solid contact material - Google Patents
Improvements relating to the conversion of fluid reactants in the presence of subdivided solid contact materialInfo
- Publication number
- GB578793A GB578793A GB12328/44A GB1232844A GB578793A GB 578793 A GB578793 A GB 578793A GB 12328/44 A GB12328/44 A GB 12328/44A GB 1232844 A GB1232844 A GB 1232844A GB 578793 A GB578793 A GB 578793A
- Authority
- GB
- United Kingdom
- Prior art keywords
- conversion
- line
- bed
- catalyst
- fluidized
- 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
- B01J8/24—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
- B01J8/38—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 fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
- B01J8/384—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 fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
- B01J8/388—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 fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only externally, i.e. the particles leaving the vessel and subsequently re-entering it
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Combustion & Propulsion (AREA)
- General Chemical & Material Sciences (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
578,793. Catalytic apparatus. UNIVERSAL OIL PRODUCTS CO. June 28, 1944, No. 12328. Convention date, Jan. 30, 1943. [Class 1 (i)] A catalytic process for the conversion of fluid reactants, e. g., hydrocarbons, employs two beds of fluidized contact material, e. g., for reaction and regeneration respectively, and particles from each bed are withdrawn and passed into the other bed while being maintained in a dense phase fluidized condition. Fig. 2 shows a reactor 55 into which the reactants are introduced by line 65, containing a fluidized catalyst bed up to level 63. Catalyst is withdrawn below the level by line 69 to regenerator 56 into which air is admitted by line 70. From the fluidized bed in the regenerator catalyst is returned to the reactor by line 75. The heat required by the endothermic conversion is supplied by the heat of the regenerated catalyst and it may be supplemented by burning fuel in the regenerator.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US578793XA | 1943-01-30 | 1943-01-30 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB578793A true GB578793A (en) | 1946-07-11 |
Family
ID=22013299
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB12328/44A Expired GB578793A (en) | 1943-01-30 | 1944-06-28 | Improvements relating to the conversion of fluid reactants in the presence of subdivided solid contact material |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB578793A (en) |
-
1944
- 1944-06-28 GB GB12328/44A patent/GB578793A/en not_active Expired
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