Vapor liquid contacting

Claim 2

In vapor-liquid contact apparatus of the cross-flow type having a column housing and at least one contact stage in said housing, said apparatus including liquid and vapor inlets to said stage, a liquid outlet from said stage, and an orificed tray mounted in said housing at said stage, means at said outlet defining a liquid retention zone on said tray, the predominant flow of vapor being along a first axis, the predominant flow of liquid through said zone being along a second axis transverse to said first axis, that improvement comprising a porous matrix in said zone having a plurality of surfaces positioned above said tray to contact said liquid and said gas flowing through said zone, said surfaces being spaced along and oriented obliquely to said first axis, and arranged in layers spaced along said second axis, said surfaces in successive layers being staggered relative to said first axis, said surfaces having a hydraulic mean diameter greater than one-half the diameter of said tray orifices, the projection of said surfaces on said tray having no open areas whose greatest dimension is more than three times the hydraulic mean diameter of the surfaces so that said surfaces deflect vapor and thereby dissipate vapor hole momentum and reduce vertical oscillations in the vapor-liquid dispersion on the tray.

Claim 3

The improvement of claim 1 wherein said first axis is perpendicular to said tray and to said second axis.

Claim 4

The improvement of claim 1 or 2 wherein said layers are parallel to said tray.

Claim 5

The improvement of claim 3 wherein said surfaces of a first layer deflect vapor in a first direction having a primary component normal to said first axis and to said second axis.

Claim 6

The improvement of claim 4 wherein said surfaces of a second layer deflect vapor in a second direction generally opposite to said first direction.

Claim 7

The improvement of claim 3 wherein said surfaces of at least one of said layers deflect said vapor in a direction having a primary component along said second axis.

Claim 8

The improvement of claim 3 wherein said surfaces of at least one of said layers deflect said vapor in a direction having a primary component opposite to the direction of liquid flow along said second axis.

Claim 9

The improvement of claim 3 wherein said apparatus includes a plurality of spaced apart vapor-liquid contacting stages, between 1 and 6 of said layers closest to said tray are closely spaced being no more than one layer thickness from adjacent layers, the lowest layer being no further above said tray than the diameter of said orifices in said tray, and the highest layer being no further from said tray than 1/2 the distance to the next higher stage.

Claim 10

The improvement of claim 8 wherein at least one layer is spaced above said closely spaced layers.

Claim 11

The improvement of claim 9 wherein said liquid outlet comprises an outlet weir, said layers above said closely spaced layers being spaced apart a distance of between 0.2 and 5 times the height of said outlet weir.

Claim 12

The improvement of claim 8 or 9 wherein the surfaces of the layer spaced furthest from said tray deflect the vapor in a direction having a primary component in the direction of liquid flow along said second axis.

Claim 13

The improvement of claim 3 wherein said apparatus includes a plurality of spaced apart liquid-vapor contacting stages, the highest of said layers being no further than 1/2 the distance to the next higher stage.

Claim 14

The improvement of claim 12 wherein a downcomer carries liquid away from said stage, at least one of said layers extending over the area above said downcomer.

Claim 15

The improvement of claim 3 wherein said layers comprise unflattened expanded metal.

Claim 16

The improvement of claim 14 wherein said expanded metal is between 12 and 18 gauge.

Claim 17

The improvement of claim 1 wherein the free area of said tray is between 6 and 40 percent of the free area of the active section of said tray.

Claim 18

The improvement of claim 1 wherein said liquid outlet comprises an outlet weir extending at least 4 inches above said tray.

Claim 19

In vapor-liquid contacting apparatus of the cross-flow type having a column housing and at least one contact stage in said housing, said apparatus including liquid and vapor inlets to said stage, and a liquid outlet from said stage, and an orificed tray mounted in said housing at said stage between said inlets, an improved inlet weir comprising a liquid inlet providing momentum to said liquid in the direction of the liquid flow path, a vapor inlet including means for mixing gas with said liquid, and giving said gas a predominant flow component in the direction of said liquid flow path, and a deflection plate above and parallel to said tray and beneath the liquid after passage through its said inlet, so that the surface of said plate facing away from said tray deflects said liquid in a direction along said tray, said vapor inlet means including an imperforate barrier sloping from above said tray downwardly toward said outlet, the upper surface of said barrier communicating with said liquid inlet to carry a stream of liquid downwardly toward said tray and said outlet, the undersurface of said barrier communiating with said vapor inlet, said imperforate barrier being spaced above said deflection plate to define therebetween a vapor entry zone onto said tray, said zone being the sole path of communication between said vapor inlet and said tray to thereby cause all vapor entering through said vapor inlet to impinge in a single layer on said stream of liquid from beneath and in the direction of said outlet.

Claim 20

In vapor-liquid contacting apparatus of the cross-flow type having a column housing and at least one contact stage in said housing, said apparatus including liquid and vapor inlets to said stage, and a liquid outlet from said stage, and an orificed tray mounted in said housing at said stage between said inlets, an improved inlet weir comprising a liquid inlet providing momentum to said liquid in the direction of the liquid flow path, a vapor inlet including means for mixing gas with said liquid, and giving said gas a predominant flow component in the direction of said liquid flow path, and a deflection plate above and parallel to said tray and beneath the liquid after passage through its said inlet, so that the surface of said plate facing away from said tray deflects said liquid in a direction along said tray, said vapor inlet means including an imperforate barrier sloping from above said tray downwardly toward said outlet, the upper surface of said barrier communicating with said liquid inlet to carry a stream of liquid downwardly toward said tray and said outlet, the undersurface of said barrier communiating with said vapor inlet, said imperforate barrier being spaced above said deflection plate to define therebetween a vapor entry zone onto said tray, said zone being the sole path of communication between said vapor inlet and said tray to thereby cause all vapor entering through said vapor inlet to impinge in a single layer on said stream of liquid from beneath and in the direction of said outlet.

Claim 21

The improvement of claim 18 wherein said liquid inlet includes a first surface which is joined at one end to said tray and extends upwardly from said tray and inwardly toward said liquid outlet, said first surface is joined at its other end to a second surface, and said second surface extends downwardly toward said outlet and said tray, to an end over orificed portions of said tray, so as to define a vapor inlet between said surfaces and said tray.

Claim 22

The improvement of claim 19 wherein said apparatus includes a plurality of layers of unflattened expanded metal, said layers being parallel to and above said tray, positioned to be in contact with said liquid and said vapor flowing through said tray.

Claim 23

The improvements of claims 19 or 20 wherein said vapor inlet communicates with a slot formed by said second surface and a third surface joined to said tray, said third surface being parallel to and below said second surface.

Claim 24

The improvements of claims 19 or 20 wherein a downcomer carries liquid to said stage, said downcomer being defined in part by a vertical apron terminating above said tray to form the entrance to said inlet weir, and said first and second inlet weir surfaces extend at least as high as the lowest point of said apron.

Claim 25

The improvement of claim 19 or 20 wherein said deflection plate is joined to said third surface.

Claim 26

The improvement of claim 19 or 20 wherein said deflection plate is joined to said second surface.

Claim 27

The improvement of claim 20 wherein said deflection plate is above at least some of said layers.

Claim 28

The improvement of claim 20 wherein said deflection plate is positioned between said tray and the layer furthest from said tray.

Claim 29

The improvement of claim 19 or 20 wherein said deflection plate is in contact with said tray.

Claim 32

The method of claim 28 wherein said outlet weir is at least 4 inches high.

Claim 33

The method of claim 28 wherein said froth height limiting means comprises a multiplicity of spaced, generally vertical baffles above said tray, said baffles extending generally in the direction of liquid flow across said tray, and being sufficiently close together to substantially reduce the amplitude of vertical oscillations in said liquid, said oscillations having a wavelength which is small relative to the width of said tray, and said tray being orificed between each pair of said baffles.

Claim 34

The methods of claims 28, 29 or 30 wherein said froth height limiting means comprises a plurality of horizontal layers of unflattened expanded metal positioned above said tray to contact said liquid and said vapor flowing therethrough.