The present invention relates to a distillation column comprising at least one cross-corrugated packing module comprising a plurality of strips with their channel orientations inverted from one strip to the next, the strip being made of a sheet material and being of the type comprising corrugations that form alternately first main peaks directed along a first direction and second main peaks directed along the opposite direction, the corrugations defining channels, each channel lying between two first or second adjacent main peaks forming edge peaks of the channel, and each channel having two channel legs that are joined together by a top main peak, the channels having a general orientation that is inclined to a general flow direction of the said liquid, the strip furthermore comprising at least one inverted portion which lies entirely within the cross section of one of the channels and which joins together the two channel legs, the inverted portion comprising a first intermediate peak oriented-in the opposite direction to the top main peak of the channel.
The term “packing” is understood to mean a device intended for mixing a phase and/or for bringing several phases flowing co-currently or countercurrently into contact with one another. A heat and/or mass exchange and/or a chemical reaction may in particular take place in the packing. One particular application of the invention lies in the columns separating gas mixtures, especially air distillation columns.
Mentioned in the prior art are air distillation installations comprising cross-corrugated packing modules, which are also called “packs”. The modules comprise corrugated metal sheets placed vertically, the corrugations of which sheets are oblique with respect to a general fluid flow direction in the installation and are inclined alternately, generally crossed at 90°, from one sheet to another.
The packing modules are slipped into the distillation column so that the sheets of one module are angularly offset with respect to the sheets of an adjacent module about the axis of the column, generally by 90° from one module to another.
To improve the exchange between a liquid and a gas, which are flowing through the packing module, it has been proposed in the prior art to have openings that are made in the corrugated metal sheets. These openings lead to a change in the flow of the gas from one side of the metal sheet of the packing to the other and improve exchange with the liquid.
A packing strip of this type is known from document EP-A-1 029 588, the corrugations of which form peaks and valleys joined together by corrugation legs defining channels. This strip includes inverted portions, also called “serrations”, which lie within each channel, each inverted portion forming a single intermediate peak. The inverted portion defines an angle of 90° with each corrugation leg to which it is joined.
When this strip is manufactured by bending a thin flat metal sheet, the material forms tears or pleats. The finished packing strip therefore deviates from its desired geometrical shape, thereby reducing the mass or heat exchange performance of the finished strip.
Document U.S. Pat. No. 4,670,196 also describes a corrugated packing strip provided with inverted portions, which has the same drawbacks.
The object of the present invention is to alleviate the above drawbacks and to propose a packing strip that is easy to manufacture from a thin flat metal sheet and results in substantial heat and/or mass exchange.
For this purpose, the subject of the invention is a column according to claim 1.
According to particular embodiments, the strip of the column according to the invention includes one or more of the following features:
The subject of the invention is also a process for manufacturing a strip made of folded metal sheet, of the type comprising corrugations that form alternately first main peaks directed along a first direction and second main peaks directed along the opposite direction, the corrugations defining channels, each channel lying between two first or second adjacent main peaks forming edge peaks of the channel, and each channel having two channel legs that are joined together by a top main peak, the channels having a general orientation that is inclined to a general flow direction of the said liquid, the strip furthermore comprising at least one inverted portion which lies entirely within the cross section of one of the channels and which joins together the two channel legs, the inverted portion comprising a first intermediate peak oriented in the opposite direction to the top main peak of the channel, the inverted portion furthermore including a second intermediate peak oriented in the direction of the top main peak, as defined above, characterized in that the process comprises the following step:
A better understanding of the invention will be gained by reading the following description, given solely by way of example and with reference to the appended drawings, in which:
The column EC comprises, at its upper end UE, a liquid inlet LI emerging in a liquid header LH which distributes the liquid over the cross section of the column EC, and a vapour outlet VO. At its lower end LE, it comprises a vapour inlet VI and a liquid outlet LO. The column EC furthermore includes a cylindrical shell S.
The column EC defines a general fluid flow direction Df, which runs vertically.
A packaging module PM1, which favours the spreading of the liquid transversely to the X-X axis, is placed in the shell S directly below the header LH. Such a module PM1 is known per se and is for example a packing module comprising a cross-corrugated packing with perforations or striations.
A plurality of packing modules PM2 according to the invention is placed in the shell S beneath the module PM1. A bottom support BS holds the packing modules PM1, PM2 in place.
Each packing module PM2 comprises a multitude of corrugated packing strips 2. The strips 2 have a mid-plane P (see
The strip 2 has two parallel edges, an upper edge 4 and a lower edge 6, which lie perpendicular to the direction Df.
The strip 2 also has corrugations 8 which form alternately first main peaks 10, directed in one direction (see
The corrugations 8 form identical but alternately inverted channels 14, each channel lying between two first 10 or two second 12 main peaks. The channels 14 are open alternately in one of the two aforementioned directions and then in the other. The intermediate main peak 12 or 10 forms the top main peak of the channel 14 in question, whereas the two adjacent peaks 10 or 12 form the channel edge peaks. Two adjacent main peaks 10, 12 are joined together by a channel leg 16 of straight section. The channels 14, and consequently the peaks 10, 12, lie along a channel direction Dc that is inclined at an angle δ to the edges 4,6 (see
In cross section, taken perpendicular to the direction Dc, as shown in
The strip 2 furthermore includes, in each channel 14, a multitude of identical inverted portions 22.
The cross section of the inverted portion 22 comprises three circular arcs 32, 34, 36. The circular arcs 34, 36 have the same radius of curvature r2 and form the second 28 and third 30 intermediate peaks, whereas the circular arc 32 has a radius of curvature r3 (>r2) and forms the first intermediate peak 26. Extending between the circular arc 32 and each of the circular arcs 34, 36 is a straight section 38 of the inverted portion 22, which straight portion is joined tangentially to each of the circular arcs 32, 34, 36. The straight sections 38 have the same length d2.
Advantageously, the circular arcs 34, 36 are joined tangentially to the channel legs 16. As a consequence, there is little stressing of the metal sheet during deformation.
Each of the two straight sections 38 makes an angle a with the adjacent corrugation leg 16.
The developed length of the inverted portion 22 is identical to the developed length of the two main straight sections 20 and of the circular arc 18. Thus, the material is not stretched, or only slightly so, during bending.
Moreover, the channel 14 has a height h which is measured between the top main peak 10 of the channel and a plane Q defined by the two adjacent main peaks 12. The distance d4 between the top main peak 10 and the first intermediate peak 26 is approximately ⅔ of the height h. In other words:
Thus, the first intermediate peak 26 lies approximately at the location of the barycentre B of the cross section of the channel. It is at this point that there is the highest concentration of mass or the highest temperature of a gas flowing in the channel 14. Consequently, the strip 2 results in substantial heat and/or mass exchange.
In addition, the channel 14 and the inverted portion 22 are symmetrical with respect to a plane of symmetry A, perpendicular to the planes P and Q, the plane of symmetry being defined by the top main peak 10 and the first intermediate peak 26.
In order for the criterion of identical developed lengths to be respected, the following geometrical condition has to be satisfied.
In the case (not shown) in which α=γ:
r1=2r2+r3.
In the case shown in
The radii of curvature r1, r2, r3 of the corrugation 8 and of the inverted portion 22 are preferably at least 1 mm and in particular at least 2 mm, thereby making it easier to form the inverted-portion 22 without material rupture.
The strip 2 according to the invention is manufactured according to a process comprising the following steps:
Owing to the presence of at least one second intermediate peak, the strip 2 is only slightly deformed at the joins 24. There is therefore little likelihood of the strip 2 tearing at these joins. Because the developed length of the corrugation 8 is the same as that of the inverted portion 22 between the joins 24, the finished strip 2 is smooth and has a thickness e which is approximately the same over its entire surface. In addition, a risk of the strip 2 fracturing during bending is low.
As a variant, the slits are cut before the flat sheet is bent, so that step (b) is carried out before step (a).
Also as a variant, steps (b) and (c) are carried out at the same time. Thus, it is unnecessary to synchronize the cutting and bending tools for the inverted portion.
According to a variant (not shown), the intermediate peak 26 is placed close to the barycentre B of the cross section of the channel 14, for example at a distance from this point B of less than 0.20 times the height h of the channel 14. Thus, the intermediate peak 26 remains within a high concentration or high temperature region.
Depending on the embodiments, the packing strip 2 according to the invention also includes the following features:
The invention also relates to a cryogenic distillation installation and in particular to an air distillation installation comprising at least one packing module as defined above.
Number | Date | Country | Kind |
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0451108 | Jun 2004 | FR | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/IB05/01509 | 5/30/2005 | WO | 6/26/2007 |