Smolders et al., 1995 - Google Patents
The operation of L-valves to control standpipe flowSmolders et al., 1995
- Document ID
- 18046191445280570966
- Author
- Smolders K
- Baeyens J
- Publication year
- Publication venue
- Advanced Powder Technology
External Links
Snippet
An extensive experimental program was carried out on group B and D powders, in L-valves of diameter between 20 and 40 mm. The particle size influences both solids' flux and pressure drop across the L-valve. The length of the horizontal transfer section has only a …
- 239000007787 solid 0 abstract description 24
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, 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
- B01J8/1872—Details of the fluidised bed reactor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, 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
- B01J8/1818—Feeding of the fluidising gas
- B01J8/1827—Feeding of the fluidising gas the fluidising gas being a reactant
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00743—Feeding or discharging of solids
- B01J2208/00769—Details of feeding or discharging
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS, 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
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Smolders et al. | The operation of L-valves to control standpipe flow | |
Herb et al. | Solid mass fluxes in circulating fluidized beds | |
Cabrejos et al. | Pickup and saltation mechanisms of solid particles in horizontal pneumatic transport | |
Kim et al. | Solids flow characteristics in loop-seal of a circulating fluidized bed | |
Song et al. | Circulation of solids and gas bypassing in an internally circulating fluidized bed with a draft tube | |
Llop et al. | Fluidization at vacuum conditions. A generalized equation for the prediction of minimum fluidization velocity | |
Olazar et al. | Study of local properties in conical spouted beds using an optical fiber probe | |
Noordergraaf et al. | Fluidization and slugging in large-particle systems | |
Milne et al. | The internally circulating fluidized bed (ICFB): a novel solution to gas bypassing in spouted beds | |
Weimer et al. | On dense phase voidage and bubble size in high pressure fluidized beds of fine powders | |
Kim et al. | Solid recycle characteristics of loop‐seals in a circulating fluidized bed | |
Cho et al. | Stochastic analysis of gas-liquid-solid flow in three-phase circulating fluidized beds | |
Cao et al. | Characterization of downflowing high velocity fluidized beds | |
Jeon et al. | Solid circulation and gas bypassing characteristics in a square internally circulating fluidized bed with draft tube | |
Daous et al. | Modeling solids and gas flow through an L-valve | |
Ahn et al. | Solid circulation and gas bypassing in an internally circulating fluidized bed with an orifice-type draft tube | |
Yin et al. | Solids holdup of high flux circulating fluidized bed at elevated pressure | |
Littman et al. | Effect of particle diameter, particle density and loading ratio on the effective drag coefficient in steady turbulent gas-solids transport | |
Satija et al. | Terminal velocity of dense particles in the multisolid pneumatic transport bed | |
Yazdanpanah et al. | Impact of size and temperature on the hydrodynamics of chemical looping combustion | |
Furchi et al. | Experimental local heat transfer in a circulating fluidized bed | |
Korbee et al. | Rate of solids and gas transfer via an orifice between partially and completely fluidized beds | |
Grieco et al. | Predicting the pressure drop across the solids flow rate control device of a circulating fluidized bed | |
Botterill et al. | Fluid-bed behaviour at elevated temperatures | |
Chandel et al. | Pressure drop and gas bypassing in recirculating fluidized beds |