Gas and liquid contact apparatus – Contact devices – Wet baffle
Reexamination Certificate
2001-01-10
2002-10-08
Bushey, C. Scott (Department: 1724)
Gas and liquid contact apparatus
Contact devices
Wet baffle
C261S114500
Reexamination Certificate
active
06460833
ABSTRACT:
FIELD OF THE INVENTION
The invention is related to a gas-liquid contacting column comprising a plurality of axially spaced contacting trays, which trays comprise one or more liquid receiving areas and one or more downcomers, which liquid receiving areas and downcomers are spaced in a bubble area and which downcomer has at its upper end a liquid receiving opening and at its lower end one or more downward directed liquid discharging openings, which openings are positioned above the liquid receiving area of the consecutive lower contacting tray and positioned at more than 10% of the tray spacing above this liquid receiving area.
BACKGROUND OF THE INVENTION
Such a column is described in U.S. Pat. No. 4,550,000. This publication describes a column provided with rectangular shaped downcomers and a bubble area. A liquid receiving area is present on the tray just below the liquid discharge openings of the downcomer of the upper consecutive tray. The downcomer is a so-called truncated downcomer because the liquid discharge openings are spaced away from the tray just below. Bubble area is present between the liquid receiving area and the downcomer opening. The liquid receiving area is covered with rectangular structures of expanded metal. These structures are meant to avoid liquid passing directly through the gas openings present in the liquid receiving area.
The column according to U.S. Pat. No. 4,550,000 is however not suited to handle higher liquid loads because the velocity of the liquid being discharged from the liquid discharge openings is of such magnitude that it will pass the rectangular structure of expanded metal and the gas openings present below said structure. For this reason one skilled in the art will typically design the receiving area on the tray without openings or with special openings like for example described in U.S. Pat. No. 5,702,647.
When trying to increase the liquid and/or gas flows of the gas-liquid contacting column as described above a maximum load will however be observed. Higher loads will result in that the column fails to function as a liquid-gas contactor or separator due to a phenomena known as flooding. Flooding is described as excessive accumulation of liquid inside the column. The well known flooding mechanisms are downcomer back-up, jet flooding and downcomer choking. These mechanisms are described in Distillation Design, Henry Z. Kister, McGraw-Hill Inc., 1992, page 267-291. According to this publication downcomer back-up is due to a build-up of liquid inside the downcomer causing the liquid to back-up on the tray leading to liquid accumulation on that tray. The liquid height in the downcomer is determined by the tray pressure drop, liquid height on the tray and frictional, losses in the downcomer and downcomer slot area. Jet flooding or entrainment flooding is caused by a too high gas velocity leading to the entrainment of liquid, either by droplets or froth, to the tray above. The liquid will accumulate and leads to flooding. Downcomer choking is caused by a too high aerated liquid velocity in the downcomer. At a certain velocity the friction losses in the downcomer and downcomer entrance become excessive, and the frothy gas-liquid mixture cannot be transported to the tray below, causing liquid accumulation on the tray. With the term froth is to be understood any gas-liquid mixture present on the tray not depending on any flow regime.
The problem to be solved by the present invention is increase the froth handling capacity of a downcomer and thus to increase the capacity of the tray.
SUMMARY OF THE INVENTION
This object is achieved with the following column. Gas-liquid contacting column comprising a plurality of axially spaced contacting trays, which trays comprise one or more liquid receiving areas and one or more downcomers, which liquid receiving areas and downcomers are spaced in a bubble area and which downcomer has at its upper end a liquid receiving opening and at its lower end one or more downward directed liquid discharging openings, which openings are positioned above the liquid receiving area of the consecutive lower contacting tray and positioned at more than 10% of the tray spacing above this liquid receiving area, wherein along the boundary of the liquid receiving area and the bubble area a weir is present.
It has been found that a column according the invention can handle a higher liquid load and therefore has an increased capacity when compared to state of the art columns. Without wanting to limit the invention by the following theory it is believed that the weir decreases the horizontal velocity of the liquid just above the tray flowing towards the downcomer opening. Because of this lower liquid velocity a more controlled entering of the liquid into the downcomer opening is achieved resulting in less downcomer choking.
A weir along the boundary of the liquid receiving area and the bubble area is described in WO-A-9839077. The difference with the present invention is that the downcomer is not a truncated downcomer as in the present invention. In other words, the liquid discharge opening of the disclosed downcomer is situated just above the tray. A next difference is that the weir is placed to create a liquid seal in order to prevent gas from entering the downcomer from below. In the present invention the weir functions as a velocity breaker and not as means to create a liquid seal.
EP-A-542538 discloses a weir situated below a downcomer liquid discharge opening. The difference with the present invention is that the downcomer is not a truncated downcomer as in the present invention. The weir disclosed in this publication serves to improve an uniform flow of the liquid on the entire bubble area.
As explained above the downcomers are so-called truncated downcomers, its lower end is preferably positioned at more than 25% of the tray spacing above the liquid receiving area of the lower consecutive tray. The tray spacing is the distance between two consecutive contacting trays in the column. Suitably the tray spacing is between 0.2 and 1 m. Generally the liquid discharge openings of the downcomer are positioned at less than 70% and preferably at less than 50% of the tray spacing above the liquid receiving area of the lower consecutive tray.
In order to avoid a liquid seal between the liquid discharge openings and the liquid receiving area the vertical height of the weir is smaller than the distance between the liquid discharge opening and the liquid receiving area. More preferably the vertical height of the weir is less than 50% of the distance between the liquid discharge opening and the liquid receiving area. A suitable vertical height of the weir is between 0.01 and 0.05 m. The vertical weir height may vary along its length. The average height of such a weir will be according to the ranges described above.
The weir can be disposed vertically or inclined. The weir may run along the entire boundary between the liquid. receiving area and the bubble area or may optionally be interrupted. The weir may be solid. Preferably openings are present in the weir.
The downcomer may for example have a square, rectangular, circular or segmental cross-section at tray level. Its lower part will normally have a corresponding form. This lower part is provided with liquid discharge openings. If these liquid discharge openings are uniformly distributed along the lower end of the downcomer, the corresponding liquid receiving area will also have the corresponding square, rectangular, circular or segmental form. The downcomer is preferably a rectangular downcomer because the advantages of the present invention are especially achieved in combination with such a downcomer design.
The liquid receiving area may be smaller than the downcomer opening area because for example the liquid discharge openings are not evenly distributed at the lower end and/or because the downcomer walls are sloped towards each other in the downward direction. Liquid discharge openings present in the lower end of a rectangular downcomer may be grouped in several different groups of
Bushey C. Scott
Shell Oil Company
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