Device for retaining particulate material in upflow tubes

Claim 2

In an upflow tube having solid particulate matter therein, the improvement comprising: a hollow member including an upwardly converging conically shaped wall, said wall having a lower rim, said hollow member being positioned for free movement in said tube with only said lower rim resting on the top of particulate material in the tube, whereby the hollow member is in contact with the particulate matter through said lower rim and provides a free flow area within said hollow member, said conically shaped wall including a plurality of openings whereby fluid upwardly flowing through the particulate matter passes through the interior of said hollow member through said openings into a space defined between the interior surface of the tube and said conically shaped wall; and a weighted member connected to said hollow member, said weighted member being positioned in said tube above the hollow member, said weighted member including portions which are spaced from the interior of the tube wall whereby fluid can pass between the tube wall and said weighted member, said weighted member applying its weight to the particulate matter through the rim of the hollow member and having a weight sufficient to retain and prevent fluidization of the particulate matter in said tube and free flow area.

Claim 3

The device of claim 1 wherein said openings in the conically shaped wall are defined by a plurality of elongated longitudinally extending slots spaced around the perimeter of the wall.

Claim 4

The device of claim 2 wherein the outer diameter of the rim of the hollow member is about equal to the interior diameter of the tube.

Claim 5

The device of claim 3 wherein the weighted member includes portions which are in contact with the interior wall of the tube.

Claim 6

The device of claim 4 wherein the weight Q of the weighted member is at least equal to Q = kg V 2 A L wherein: k = factor having numerical value 0.0035 sec 2 /in 2 g = density of fluid at operating condition lbs/ft 3 V = velocity of fluid at operating condition ft./Sec A = inner cross sectional area of the catalyst tube in 2 L = length of catalyst bed ft.

Claim 7

In an upflow tubular catalytic steam reformer, including at least one tube having catalyst therein, the improvement comprising: a hollow member including an upwardly converging conically shaped wall, said wall having a lower rim, said hollow member being positioned for free movement in said at least one tube with only said lower rim resting on the top of catalyst in the tube, whereby the hollow member is in contact with the catalyst through said lower rim and provides a free flow area within said hollow member, said conically shaped wall including a plurality of openings whereby fluid upwardly flowing through the catalyst passes through the interior of said hollow member through said openings into a space defined between the interior surface of the tube and said conically shaped wall; and a weighted member connected to said hollow member, said weighted member being positioned in said at least one tube above the hollow member, said weighted member including portions which are spaced from the interior of the tube wall whereby fluid can pass between the tube wall and said weighted member, said weighted member applying its weight to the catalyst through the rim of the hollow member and having a weight sufficient to retain and prevent fluidization of the catalyst in said tube and free flow area.

Claim 8

In an upflow tubular catalytic steam reformer, including at least one tube having catalyst therein, the improvement comprising: a hollow member including an upwardly converging conically shaped wall, said wall having a lower rim, said hollow member being positioned for free movement in said at least one tube with only said lower rim resting on the top of catalyst in the tube, whereby the hollow member is in contact with the catalyst through said lower rim and provides a free flow area within said hollow member, said conically shaped wall including a plurality of openings whereby fluid upwardly flowing through the catalyst passes through the interior of said hollow member through said openings into a space defined between the interior surface of the tube and said conically shaped wall; and a weighted member connected to said hollow member, said weighted member being positioned in said at least one tube above the hollow member, said weighted member including portions which are spaced from the interior of the tube wall whereby fluid can pass between the tube wall and said weighted member, said weighted member applying its weight to the catalyst through the rim of the hollow member and having a weight sufficient to retain and prevent fluidization of the catalyst in said tube and free flow area.

Claim 9

The steam reformer of claim 6 wherein said openings in the conically shaped wall are defined by a plurality of elongated longitudinally extending slots spaced around the perimeter of the wall.

Claim 10

The steam reformer of claim 6 wherein the outer diameter of the rim of the hollow member is about equal to the interior diameter of the at least one tube.

Claim 11

The steam reformer of claim 6 wherein the weighted member includes portions which are in contact with the interior wall of the tube.

Claim 12

The steam reformer of claim 6 wherein the weight Q of the weighted member is at least equal to Q = kg V 2 A L wherein: k = factor having numerical value 0.0035 sec 2 /in 2 g = density of fluid at operating condition lbs./ft 3 V = velocity of fluid at operating condition ft/Sec. A = inner cross sectional area of the catalyst tube in 2 L = length of catalyst bed ft.