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Aktiebolag Carl Munters

Gunter Ernst

Dieter Wurz

Edmund Baer

Hans Dittrich

Wilhelm Roller

An evaporative cooler which for the purpose of cooling a fluid flowing within at least one duct (1) evaporates a substance on the outside of said duct, said substance being supplied in liquid form through at least one conduit, is characterized by at least one liquid connector (7) for controlled passage of the liquid from the conduit (6) onto the outside of said duct (1), wherein the outside of the duct (1) is covered by a porous capillary layer (2) into which the liquid connector(s) (7) open(s). The capillary layer (2) may be surrounded by a liquid barrier (3).

Evaporative cooler

In an apparatus for cooling of cooling water trickler plates are arranged essentially in parallel. Along one side of each trickler plate water sprayed from the top trickles down, while the other side is kept dry. Thus a pair of adjacent trickler plates each forms a duct through which the cooling air flows. The trickler plates are provided with depressions in the wet side protruding from the dry side in order to increase the dry cooling effect with respect to the wet cooling effect.

Apparatus for cooling cooling water

A cooling tower is provided with a crown inwardly tapered towards the upper discharge opening defined by the upper rim of the crown to create a pressure differential greater on the inside than on the outside of the crown to inhibit cold air break-ins in still air or winds of low velocity. The cooling tower shell is tapered inwardly in the crown region and the angle between the tangent to the internal contour and the vertical in said crown region of the shell is preferably chosen to be not smaller than results from the following equation: ##EQU1## in which .alpha. is the angle in question, g is the acceleration due to gravity, .rho..sub.a and .rho..sub.i are the gas densities inside (i) and outside (a) of the cooling tower, z is the vertical coordinate, d.sub.o and d(z) are the diameters of the internal shell contour at the level z=o and z, respectively, and w.sub.o is the gas velocity at the level z=o. By this equation, the cooling tower designer may provide for shell contours which for all sizes of cooling towers on the one hand safely prevents cold air penetration and on the other hand warrants a minimum of draft losses in operation of the cooling tower. To reduce the effect of side winds of high velocity, the crown may carry a wind-deflector ring with an upwardly-inclined deflecting surface to inhibit the creation of a vortex over the tower.

Cooling tower

A cooling tower is provided with a crown inwardly tapered towards the upper discharge opening defined by the upper rim of the crown to create a pressure differential greater on the inside than on the outside of the crown to inhibit cold air break-ins in still air or winds of low velocity. To reduce the effect of side winds of high velocity, the crown may carry a wind-deflector ring with an upwardly-inclined deflecting surface to inhibit the creation of a vortex over the tower. The tower may be suspended by cables from a central mast, and the wind-deflector ring may be suspended by separate cables from the mast, these latter cables being tensioned between the masthead and the lower part of the crown by means of a support ring arranged at the base of the wind-deflector ring.

An apparatus for spraying trickler plates with cooling water, particularly in cooling towers, comprises spray channels 7,8 which are formed to be smoothly continuous and which touch or pass through the upper end sections of the trickler plates 1. The trickler plates are provided in the upper areas with a surface pattern 27 for uniform distribution of the cooling water. The spraying apparatus avoids a spacing between the spray channels and the trickler plates and provides for easy manufacture maintenance, particularly for an easy cleaning of the spray channels 7,8 (FIG. 5).

Apparatus for spraying trickler plates with cooling water

A water cooling tower and method which provides for both wet and dry cooling within the same vertical space and significantly reduces the discharge of water particles out of the tower. Water is deposited on one side of each of a plurality of trickler plates and flows downwardly under the influence of gravity substantially undisturbed as a low speed film. Air flows at low speed by natural draught in a substantially undisturbed path on the other side of each of the plates. Important dimensional ratios and construction details are disclosed.

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Karlsruhe, Germany

Gunter Ernst