Packing for heat-exchange and mass-transfer columns

Details Packing for heat-exchange and mass-transfer columns Packing for heat-exchange and mass-transfer columns

2001-06-26

2003-01-28

Bushey, C. Scott (Department: 1724)

Gas and liquid contact apparatus

Contact devices

Wet baffle

C261S113000, C261SDIG007

Reexamination Certificate

active

06511053

ABSTRACT:

The invention relates to packing sheets designed with a cross-channel structure, and to packing for heat exchange and mass transfer between a liquid and a gas in a column containing such packing sheets.
In the distillative work-up of product mixtures, the best results are generally achieved in so-called countercurrent distillation, also known as rectification, i.e. a distillation process in which the liquid flows from top to bottom and the vapor from bottom to top in the column, with the lower-boiling components accumulating in the vapor and the higher-boiling components in the liquid.
This mass and heat transport is increased by elements built into the column, such as column trays, packing elements or structured packing, which ensure an adequate contact time of the phases and a sufficiently large phase interface. However, these column internals and the downflowing reflux associated therewith give rise to a flow resistance for the vapor in the column, known as the pressure loss. For a given column geometry, i.e. diameter and column height, the pressure loss of the column depends very heavily on the type of column internals in addition to the type and amount of compounds to be rectified.
For the separation of substance mixtures which require high separation performance, use is made of rectification columns with internals comprising stacked metal structures. These packings, which have a systematic structure in a regular geometry with defined passage zones for the countercurrent phases, are distinguished by higher loading capacity, better separation action and a lower specific pressure loss compared with all other internals. They are therefore employed in all vacuum rectifications in which, owing to the heat sensitivity of the mixture to be separated, restriction of the column pressure loss is particularly important. In the case of structured packing, physical shapes with a cross-channel structure which consist of metal sheets, expanded metal or wire meshes have proven particularly successful, for example metal mesh packing of the BX and CY type from Sulzer A G, CH-8404 Winterthur (cf. company publication “Trennkolonnen für Destillation und Absorption” [Separating Columns for Distillation and Absorption] from Sulzer A G) and metal mesh packings with a similar action from other manufacturers, for example Montz-Pak type A3, BSH or B1 from Montz GmbH, D-40723 Hilden.
A diagrammatic representation of such columns is given, for example, on page 103 of the reference book “Thermische Trennverfahren” [Thermal Separation Methods] by K. Sattler, VCH Verlagsges mbH, Weinheim (Germany), 1988. For further details of the rectification of substance mixtures, we refer to this reference book by Klaus Sattler, pages 101-225, in particular 120-160 and 199-214.
In these packings with a cross-channel structure, the starting material is usually additionally provided with passage apertures, for example with circular holes having a diameter of from about 4 to 6 mm, in order to raise the flooding point of the packing and to facilitate higher column loading.
In this connection, the term flooding point is taken to mean the gas or liquid volume per time and cross-sectional area in which the downflowing liquid builds up in or above the bed to complete overflow or is entrained by the gas stream. Exceeding of this load results in a rapid reduction in the separation efficiency and a steep increase in the pressure loss (details in “Thermische Trennverfahren” [Thermal Separation Methods] by K. Sattler, VCH Verlagsges mbH, Weinheim (Germany) 2nd Edition, 1995, pp. 240 ff.).
The passage apertures are uniformly distributed over the packing sheet.
The angle which the kinked areas (referred to as kink areas below) form to one another, referred to below as the kink angle (&ggr;), is usually from about 60° to 90°. Structured packing with packing sheets having a smaller kink angle is rather unusual. An exception is formed by WO 98/50752, which describes structured packing with packing sheets which have a smaller kink angle of less than 67°.
The packings are combined to form individual beds with a depth of from about 0.15 to 0.25 m. Each bed is built up from a multiplicity of individual layers of kinked sheets, expanded metals or meshes, with the kinks in most designs running in straight lines and usually being inclined at an angle of from 30 to 45° to the vertical, i.e. to the column axis. DE-A 196 05 286 describes a special development of packings for use in the separation of particularly heat-sensitive substances in which this angle is reduced to from 0 to 25°, preferably from 3 to 14°, in order to lower the pressure loss of the packings as far as possible in the case of applications in a high vacuum (head pressure about 1 mbar).
The previously known packings have the disadvantage that the liquid film on the packing sheets becomes unstable even at relatively low liquid loadings. In general, the flooding point is lower the greater the inclination of the kinks to the column axis.
It is therefore an object of the present invention to indicate packings which facilitate a greater inclination of the kinks to the column axis and a higher flooding point in respect of a certain fluid.
We have found that this object is achieved by a packing sheet having straight-line kinks which divide the packing sheet into kink areas which have a width a, measured from kink edge to kink edge, and passage apertures. In the packing sheet according to the invention, a proportion X of at least 60% of the passage apertures has a separation b of at most 0.4 a from the lower kink edge.
Like the packing sheets of the previously described packings, a packing sheet according to the invention has straight-line kinks. These kinks divide the surface of the packing sheet into sub-areas, which are referred to for the purposes of the invention as kink areas. The width of these kink areas, which corresponds to the separation of two adjacent kink edges, i.e. is measured from kink to kink, is denoted by a. Passage apertures are located on the kink areas, and can also bridge kink edges. The passage apertures can have any conceivable geometry, in particular can be designed as circular holes or as slots, slots being preferred. Slots are passage apertures of rectangular or virtually rectangular geometry with a length/width ratio of greater than 1:1, preferably from 5:1 to 1:1, in particular from 4:1 to 2:1, especially from 3:1 to 2:1, but generally less than 10:1. The longer side of the slot preferably runs parallel or essentially parallel (±10°) to the kink edges. The separation of the passage aperture from a kink edge, b, is measured from the point of the passage aperture which has the greatest separation from the kink edge. These passage apertures may be distributed stochastically over the kink area in accordance with the rules according to the invention, in which case the separation b of a passage aperture would then be different in each case. Furthermore, the passage apertures may be arranged in accordance with certain rules—such as equal separation along a spatial direction. At separation b from the kink edge, passage apertures are only provided on one side of the kink edge—the bottom kink edge—and are not provided on the other side of the kink edge. It is furthermore possible for some of the kinks to have no passage apertures. At least 60% of the kinks of a packing sheet, preferably 80%, in particular 90%, especially 100% of the kinks should have passage apertures on one side.
The packing sheet according to the invention differs from the known packing sheets in that a proportion X of at least 60% of the passage apertures has a separation b of at least 0.4 a from a kink edge. X adopts preferred values of at least 70%, 80% or 90%, where, in a particularly preferred embodiment, X is 100%. The separation b is preferably less than or equal to 0.3 a, 0.2 a or 0.1 a; in particular, the separation is about 0.25 a. Preferably, no passage aperture bridges a kink edge.
In a further embodiment of the packing sheet according to the in

Affiliated with

Also associated with

Rating

Packing for heat-exchange and mass-transfer columns does not yet have a rating. At this time, there are no reviews or comments for this patent.

If you have personal experience with Packing for heat-exchange and mass-transfer columns, we encourage you to share that experience with our LandOfFree.com community. Your opinion is very important and Packing for heat-exchange and mass-transfer columns will most certainly appreciate the feedback.

Rate now

Comments { 0 }

Profile ID: LFUS-PAI-O-3069800