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Publication numberUS2055162 A
Publication typeGrant
Publication dateSep 22, 1936
Filing dateJan 18, 1934
Priority dateJan 18, 1933
Publication numberUS 2055162 A, US 2055162A, US-A-2055162, US2055162 A, US2055162A
InventorsAugust Weber Friedrich
Original AssigneeAugust Weber Friedrich
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Chamber or tower filled with filling material
US 2055162 A
Abstract  available in
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Claims  available in
Description  (OCR text may contain errors)

F. A. Wimax-:R

Sept. 22, 1936.

CHAMBER OR TOWER FILLED WITH FILLING MATERIALI Filled Jan.'` 18, 1954 filo Patented Sept. 22, 1936 UNiTED STATES CHARIBER OR TOWER FILLED WITH FILLING MATERIAL Friedrich August Weber, Duisburg, Germany Application January 18, 1934, Serial No. 707,224 In Germany January 18, 1933 Claims. (Cl. 261-94) In order to bring liquids in towers or reaction 4chambers into the most intimate contact possible with gases or vapors, such towers and vchambers are filled with filling materials of the most varied kind and shape or the filling materials are so disposed in regular arrangement that the rrigating liquid is tho-roughly distributed and several channels and contact surfaces are offered to the gas stream, without an accompanying excessive increase of the resistance of the lled chamber to the passage of the gas. Fillings or arrangements are known which fulfill this purpose relatively completely.

It has, however, been found that if the height of such towers and reaction chambers is increased beyond a certain extent, such increase `in height does not lead to a proportionate increase in effect. This is due to the fact that the distributing effect ofthe filling on the downwardly trickling liquid causes more and more of the liquid to fiow downward along the peripheral wall. In order to make a complete use of the upper part of a tower, the irrigating liquid must i which has passed to the peripheral walls and is trickling therealong. Hence, a constantly increasing part of the liquid fiows downward adjacent the side walls. This quantity of liquid is almost completely lost so f ar as irrigation and Ythe intended action is concerned, and the centre of the chamber becomes more and more deprived of irrigating liquid. `This disadvantage becomes specially marked when' the operation is carried out in countercurrent and, consequently, a great height of the chamber or tower is of particular value, as for example in enriching operations, washing ammonia out of coal gas and the like.

The principal object of this invention is to overcome this disadvantage.

According to the invention the liquid is con- Veyed away from the walls towards the centre, by filling the towers or reaction chambers so full with filling materials, that their surfaces or principal surfaces effect a unilateral deflection of the downwardly trickling liquid towards the'axis of the tower, and thus counteract the tendency of theirrigating liquid to force itself against the walls.

The surfaces or principal surfaces thus form an acute angle from above with the axis of the tower.

All Vfilling materials with surfaces having dif-L I ferent dimensions in different directions are suitable but spherical or approximately spherical or cubical filling materials are unsuitable.

The introduction of the filling materials, by:`

l pouring in such a way that the surfaces or printhe axis of the tower or chamber.

This method of pouring adjacent the walls with an angle of slope increasing from the cenn tre towards the wall, is suitable for all filling ma-4 terials, which are plate-shaped or elongated and for ring-shaped filling materials which are greater in height than in diameter.

In the case of other filling materials, the same; effect may be obtained by pouring from the axis outwards, i. e. in the case of ring-shaped filling bodies, which are less in height than in diameter.

If such filling bodies were poured adjacent the wallsjthe deecting surfaces, i. e. the cylindricalV surfaces, would be so arranged that they would deflect the current of liquid towards the walls.

The introduction of the filling materials by pouring offers no difficulties, it being possible to a slight extent to form the initial inclined sur-V faces at the start by disposing the filling materials accordingly. Y

If these filling materials are allowed to slide down over their own inclined surfaces, the chief planes of these plates all become more or less` disposed in the direction of the slope and will of course produce a very considerable deviation, which may in certain circumstances even become excessive. This deviation would more- ,overv in certain circumstances have the disadvantage, that the gas stream would be considerably deviated towards the outer side of the holthe outer circumference is lens-shaped or oval. Fragments of coke or stone may be employed, provided they are oblong in shape or deviate from the spherical. These filling materials may of course also be hollow and provided with perforations, indentations and the like, provided they have such a shape that on being poured in obliquely they impart a deviation fromV the vertical'to entering jets of liquid. Thus, for example, lling rings may also beemployed, the height of which is greater than the diameter. The filling of a hollow chamber in this manner is no-t appreciably more costly than the method hitherto usually emplo-yed.

Finally the residual inner cone is levelled off by filling up from the outer edges. K Illustrative forms of practicing the invention are shown in the accompanying drawing in which:

Figure 1 is an upright section through a trickle tower or chamber, indicating the ar- 'rangement of the filling material therein and 7 the method of placing such material.

Figure 2 is an enlarged view of the portion indicated by dotted lines on Figure 1.

Figure 2a is asimilar fragmentary section showing a diiferent type of forming material.

Figure 3/is a view similar to Figure 1, showing -a layer-wise arrangement of such material.

In the drawing, the trickle tower or chamber has the upright walls I and a bottom wall Il.

Y When charged, the chamber is usually covered fao at the top by a member l2 as indicated in Figure 3. Gas inlet and outlet conduits G and E operate in conjunction with liquid inlet and outlet conduits L and D.

`In Figure 1, the entire chamber space is Ycharged with a filling material l5 which com- VVprises a mass of bodies each having a greater from the apex ofthe pile toward its lower chamber.

margin. Y

This charging is accomplished according to Figure 1 by depositing the bodies through the pouring device I6 in the direction of arrows a, so that the material is deposited adjacent the walls I0 and the slope is formed by the sliding of the bodies downwardly and toward the axis of the chamber, the bodies coming to rest and providing, so to speak, strata or layers in which the bodies incline downwardly away from the walls and toward the center or axis of the chamber. The pouring device i6 may initially be within the chamber and close to its bottom to avoid fragmentation or breaking of the bodies as they are deposited. It can be carried regularly around the chamber during the depositing operation, while withdrawing it in an upward direction as the annular pile is formed with the conical surfaces of repose of the material forming in the directions indicated by the lines within the Ultimately, the pouring device i6 is entirely withdrawn from the filled portion of the chamber and then moved in the direction of arrow b toward the axis so that the final chargby gravitational fall in a downward direction as indicated by the arrows a, and at points or lines along the chamber walls, so that the individual bodies slide downwardly over one another with their greater dimension substantially in the direction of the prevailing surface of repose.

Thus, a regularity of position is attained by the individual bodies, so that their deflecting surfaces receive the trickling liquid and. deect it toward the axis or center, and thus counteract Y the tendency of the trickling liquid to move toward the walls of the chamber and assure a uniform distribution of the liquid in its downward trickling or irrigating movement.

Figure 2 is a conventional view indicating the tendency of the bodies when of disk or platelike shape to arrange themselves in a substantially regular order as described herein.

A similar arrangement is attained by bodies of lens-shape, when similarly deposited, as shown in Figure 2a.

In Figure 3, the trickle chamber or tower is charged with successive layers of material. The layers 2i) are of material which has no unilateral deflecting power, while the intermediate layers 2i are deposited in the manner described for the charging material I5 of Figure 1, and thus have a unilateral delecting capacity. With this arrangement, the layers 2i! tend to cause the liquid to move toward the walls, but operate to distribute the ascending gases regularly, while the layers 2| tend to deiiect the liquid toward the axis, but in some instances may produce an outward deflection of the gases if the resistance to gas movement, of such layers 2|, is not Sunicient to assure a uniformity of distribution.

Further, in order to produce a definite degree of deviating eifect, lling materials, which fulfill these requirements, may be mixed with filling materials which do not fulfil these require-'40 the proposed vmethod of pouring with a filling.

material having a pronounced plate shape. If

Y the filling offers an appreciable resistance to the passage of the gas, this will counteract the tendency of the gas to force itself against the wall. Particularly in the case of towers and cham-= bers of large diameter, a counter eifect may also be obtained by disposing the gas outlet in the centre of the tower. Finally, if the resistance of the filling to the movement of the gas must not be considerable, individual layers of finer filling the chamber, which comprises preparing filling bodies each having a greater dimension in one direction than in a direction at a right angle thereto, and pouring the bodies into the chamber to form a pile therein, the individual bodies sliding upon one another along the angle of repose of the pile being formed and coming to rest with said greater dimension in a plane parallel to said angle of repose.

2. A process for illing a trickle chamber with a mass of bodies presenting surfaces in definite relative positions for directing the ow of liquid through the chamber, which includes preparing lling bodies each having a greater dimension in one direction than in a direction at right angles thereto, and pouring the bodies into the chamber from several points adjacent the walls of the chamber, so that the individual bodies slide upon one another and determine an angle of repose, each body arranging itself with the greater dimension thereof coming to rest in a direction substantially parallel to the angle of repose for providing deflecting surfaces for counteracting the tendency of the liquid to move toward the walls of the chamber.

3. A trickle chamber structure comprising upright confining walls and a lling comprising a mass of slidable bodies each having at least one dimension thereof greater than a dimension at right angles to said one dimension and arranged with said greater dimension substantially in the direction of the angle of repose of said bodies when poured to form a pile, the surfaces of said bodies which provide paths of preferential ow for the trickling liquid being inclined downward and inward and constantly tending to deect the flow toward the center of the chamber, whereby to counteract the tendency of the liquid to move toward the walls.

4. A trickle chamber structure as in claim 3, in which the lling comprises a plurality of masses of slidable bodies having the said directed arrangement, said masses forming vertically spaced layers, the space between each two such layers being occupied by a lling material in non-directed arrangement for distributing ilowing gases. l

5. A trickle chamber structure comprising upright conning walls and a filling comprising a mass of slidable plate-like bodies having greater dimensions in one plane than in the direction of thickness at right angles to said plane, said bodies presenting surfaces inclined upwardly toward the walls and being located with the said planes substantially in the direction of the surface of repose of said bodies when poured to form a pile, the surfaces of said bodies providing paths of iiow for the trickling liquid constantly tending away from the walls whereby to counteract the tendency of the liquid to move toward the walls.

FRIEDRICH AUGUST WEBER.

Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3914351 *Mar 2, 1973Oct 21, 1975Mass Transfer LtdPacked tower and method of operation
US3957931 *Feb 26, 1974May 18, 1976Mass Transfer LimitedFluid-fluid contact method and apparatus
US3959419 *Sep 6, 1973May 25, 1976Fritz W. Glitsch & Sons, Inc.Vapor-liquid contact method
US4002705 *Jun 10, 1975Jan 11, 1977Mass Transfer LimitedFluid-fluid contact apparatus
US4126539 *Dec 5, 1977Nov 21, 1978Mobil Oil CorporationMethod and arrangement of apparatus for hydrogenating hydrocarbons
US4195043 *Jan 17, 1979Mar 25, 1980Norton CompanyRandomly dumpable self orienting spiral packing elements
US5130062 *Jul 12, 1991Jul 14, 1992Sulzer Brothers LimitedPacking for a material and heat exchange column
US5237823 *Mar 31, 1992Aug 24, 1993Praxair Technology, Inc.Countercurrent transfer contacting of descending liquid mixture and ascending vapor mixture in rectification column
US5514304 *May 29, 1992May 7, 1996Sulzer AgPacking for a material and heat exchange column
US5688444 *Jul 29, 1996Nov 18, 1997Norton Chemcial Process Products CorporationTower packing element
US5718846 *Jun 14, 1996Feb 17, 1998Bayer AktiengesellschaftProcess for mass transfer using fluidized bed bodies
US5997173 *Feb 24, 1999Dec 7, 1999Koch-Glitsch, Inc.Packing brick and method of constructing packing bed in exchange column using same
US6089549 *Sep 25, 1997Jul 18, 2000Koch-Glitsch, Inc.Exchange column structured packing bed having packing bricks
US6666436Sep 25, 2002Dec 23, 2003Beco Engineering Co.Mixed-size packed beds
US7566428 *May 9, 2005Jul 28, 2009Saint-Gobain Ceramics & Plastics, Inc.Bed support media
US8524164 *Aug 15, 2007Sep 3, 2013Crystaphase Products, Inc.Filtration, flow distribution and catalytic method for process streams
DE19733275A1 *Aug 1, 1997Feb 11, 1999Univ Dresden TechInserts for fluid flow passages used in e.g. heat exchange systems
DE19733275C2 *Aug 1, 1997Feb 8, 2001Univ Dresden TechRegenerator oder Adsorber für die Wärme- und/oder Stoffübertragung und Speicherung bei laminaren Strömungsverhältnissen
Classifications
U.S. Classification261/94
International ClassificationB01J19/30, B01D47/06
Cooperative ClassificationB01J19/30, B01D47/06, B01J2219/30211, B01J2219/30215
European ClassificationB01D47/06, B01J19/30