Abstract: A reactor configuration for fluidized bed reactors in which large exposed fixed surface area per unit reactor volume is required. The configuration uses a serpentine or hairpin bend arrangement of continuously connected and communicating thin channels, with the containing surfaces of these channels being vertical. This configuration enables uniform fluidization of particles throughout the cross-sectional area of the reactor and facilitates dispersal of membrane surfaces, heat transfer surface and baffles in gas-solid fluidized bed reactors.

Abstract: A method of assisting with fluidization of difficult-to-fluidize materials and to improve the quality of fluidization of particles in general. The use of either helium or hydrogen as a gaseous fluidization aid. The addition of hydrogen and/or helium to the fluidization agent or the substitution of part of the fluidizing gas by hydrogen or helium as a fluidization agent is disclosed. The advantageous and desirable effect is that the fluidization quality of the particles is significantly improved.

Abstract: A dispensing apparatus for the dispensing of ultra-fine particles on a dry basis in a reproducible manner. The apparatus includes a first gas-solids suspension chamber having particle fluidization means adapted thereto, and a conduit adapted between the first gas-solids chamber and a second gas-solids chamber for communicating via at least one particle orifice particles between the chambers. A high velocity gas stream provides a pressure difference between the chambers whereby a low pressure zone is created within the conduit thereby drawing in particles from the first gas-solids suspension chamber into the second gas-solids suspension chamber via the conduit. The apparatus further includes a combination of a withdrawal feed and a solenoid valve to direct particles from the second gas-solids suspension chamber into a collection area.

Abstract: Hydrogen gas is generated in a fluidized bed reactor by reacting gases namely steam and a hydrocarbon gas such as methane or natural gas in a fluidized bed of particulate catalytic material. The catalytic material is fluidized by injecting the mixture of the reacting gases at the bottom of the bed. Hydrogen generated within the bed is removed via a selectively permeable membrane that extends through the bed and through a freeboard area above the bed. The reaction is endothermic and therefore heat to maintain the bed at the desired temperature is added as required. Preferably a separator separates particulate catalytic material entrained in the gases in the freeboard area and delivers the particulate material separated from the gas back into the bed.