Abstract The reaction gas throughout of the supply duct feeding gas to the bottom of a fluidized bed reactor of the kind shown in U.S. Pat. No. 4,153,004, issued May 8, 1979, is increased by providing the reaction gas supply tube in the form of a bundle of tubes of small cross-section of about 2 mm diameter. Subdivision of the supply tube into hexagonal ducts in honeycomb arrangement maximizes the useful cross-sectional area of the supply tube. With the smaller elemental tube diameters, a higher rate of flow is maintainable without loss of laminar flow behavior, which behavior is maintained in the jet issuing from the subdivided reaction gas supply duct as it flows towards the constricted entrance into the fluidized bed container while being surrounded by a sheath of inert carrier gas supplied by an annular duct surrounding the reaction gas tube. It is thus possible to increase the input of reaction gas without increasing the diameter of the jet or loss of the laminar flow characteristics necessary to prevent the reaction gas from making deposits that would interfere with the introduction of gas into the bottom of the bed.
A method of achieving an increased rate of laminar gas flow in the limiting range for laminar gas flow in a straight terminal portion of an open-ended duct and the length of the laminar portion of a jet issuing therefrom, which consists of providing said terminal portion of said duct with subdividing walls for subdividing the interior thereof into a plurality of separate ducts of substantially equal cross sectional area over a straight terminal portion of said duct having a length (l) which is not less than 3% of the product (Re·d 2 ) obtained by multiplying the diameter of one of the separate ducts (d 2 ) by the Reynolds number (Re) of the gas flow therein.
Claim 2
Independent Claim
118 words
A method of achieving an increased rate of laminar gas flow in the limiting range for laminar gas flow in a straight terminal portion of an open-ended duct and the length of the laminar portion of a jet issuing therefrom, which consists of providing said terminal portion of said duct with subdividing walls for subdividing the interior thereof into a plurality of separate ducts of substantially equal cross sectional area over a straight terminal portion of said duct having a length (l) which is not less than 3% of the product (Re·d 2 ) obtained by multiplying the diameter of one of the separate ducts (d 2 ) by the Reynolds number (Re) of the gas flow therein.