Gkss-forschungszentrum Geesthacht Gmbh

Gesellschaft Fur Kernenergieverwertung in Schiffbau Und Schiffahrt Mbh

Gsk Forschungszentrum Geesthacht Gmbh

Walter Hilgendorff

Gerhard Kahn

Karl W Boddeker

Jurgen Kaschemekat

Axel Wenzlaff

Frauke Jordt

Gunter Luhrs

In a device for filtering and separating fluids, a plurality of disc-like spaced flow guide elements are disposed in a stack in spaced relationship with filter elements disposed in the spaces between the flow guide elements to which fluid can be supplied through inlet openings to flow over the surfaces of the filter elements. Each flow guide element defines at one end a flow opening for the passage of fluid and at least one channel formed in the flow guide element so as to extend adjacent the opening in a direction transverse to the flow of the fluid from the opening into the space between the flow guide elements to promote fluid flow distribution over the width of the flow path through the device.

Filtration apparatus having channeled flow guide elements

Device for separating mixtures using stacked spaced membrane elements

An apparatus for separating fluid mixtures by membrane elements, which are spaced and arranged into a membrane element stack via a supporting frame that comprises outer and inner rings, whereby the membrane elements have a boring for draining a permeating substance. The boring has an inlet port for introducing the mixture into the apparatus and an outer port for the retained substance as well as the permeating substance. In mixture compartments, formed by the membrane elements between said inner and outer rings, the mixture to be separated flows past areas of the membrane elements, having a constant effectiveness, whereby the flow cross-sections of the mixture compartments vary from the introduction port to the exit port of the membrane stack. All inner and outer rings of the membrane element stack have identical dimensions, and the differing cross-sections in the mixture compartments are adjustable at least by varying the width of the membrane elements.

Apparatus for separating mixtures by spaced stacked membrane elements

An apparatus for filtering and separating flow medium by reverse osmosis, ultrafiltration, and microfiltration. A plurality of essentially sheet-like filter elements are disposed next to, and spaced from, one another so a to form flow chambers for the flow medium. Filtrate that is produced is withdrawn at the end face of at least one hole formed in a filter element and disposed at essentially right angles to the planar surface thereof. A plurality of sheet-like, self-supporting filter element carriers that are successively arranged have disposed essentially laminarly thereon the filter elements, with the filter element carriers being spaced from one another at such a distance that there is formed between each two facing filter elements one of the flow chambers. Disposed in each flow chamber, between two facing filter elements, is a disk that imparts turbulence to flow medium in the flow chamber.

Apparatus for filtering and separating flow medium

A fluid treating apparatus has a plurality of chambers arranged in a stack along the apparatus axis; inlet and outlet ports in end plates as well as a central channel for introducing fluid into and removing fluid from the apparatus; and a plurality of fluid-impervious diaphragms situated in a spaced relationship in the chambers in an orientation generally perpendicular to the axis. The fluid is guided along the diaphragms generally radially inwardly. The apparatus further has a plurality of support frames arranged in a stack along the axis. Each support frame includes an inner ring spacedly surrounded by an outer ring. The radially inner face of the outer ring and the radially outer face of the inner ring of each support frame together define radially outer and radially inner boundaries, respectively, of the chambers. The radially outer faces of the outer rings together form an outer wall face of the apparatus, and the radially inner faces of the inner rings surround the central channel. Each outer ring has a supporting face engaging a radially outer marginal surface portion of an adjoining diaphragm, and each diaphragm has a central aperture in axial alignment with each inner ring and a passage at a radially outer part for allowing flow of fluid axially through each diaphragm.

Diaphragm-equipped fluid treating apparatus

An apparatus for the separation of solutions by pervaporation includes a raw solution chamber through which a raw solution is conducted from which a part is to be separated, a permeation chamber disposed adjacent the raw solution chamber but separated therefrom by a membrane which permits evaporation therethrough of part of the solution into the permeation chamber from which the vapors are removed, a heating structure arranged adjacent the raw solution chamber in direct contact with the raw solution therein for replenishing to the solution the heat consumed by pervaporation of part of the solution through the membrane. The raw solution chambers have closely spaced solution supply and discharge openings along opposite walls to provide laminar flow therethrough in one direction and the pervaporation chambers have discharge openings closely spaced along opposite side walls oriented normal to the orientation of the raw solution supply and discharge openings so as to rapidly remove from the pervaporation chamber any pervaporate and to remove it in a direction normal to the flow direction of the raw solution through the raw solution chamber.

Apparatus for the separation of solutions by pervaporation

Apparatus for desalinating water by reverse osmosis, having a series of pus discs each covered on both sides by a membrane, and compressed at their edges between respective pairs of a stack of module plates which are identical and which each consist of two mirror image halves, alternate module plates in the stack being rotated through 180.degree.. A zig-zag flow path through the stack is thereby provided with desalinated water passing by reverse osmosis into the porous discs and hence radially outward of the stack for collection.

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Tespe, Germany

Walter Hilgendorff