Gea Mechanical Equipment Gmbh

Westfalia Separator Ag

Gea Westfalia Separator Group Gmbh

Gea Westfalia Separator Gmbh

Kathrin Quiter

Wilfried Mackel

Thomas Bathelt

Andreas Penkl

Thomas Kleimann

Stefan Terholsen

Rüdiger Göhmann

Andreas Schulz

Jürgen Mackel

Marie-Theres Sedler

Ludger Horstkötter

Ludger Thiemann

Jürgen Hermeler

Juergen Starke

Tim Hundertmark

Angelika Voltmann

Jürgen Linnemann

Stefan Pecoroni

Bernd Terwey

Markus Hüllmann

Andrej Michel

Kai Helmrich

Julian Koenig

Jürgen Starke

Julian Konig

Wilhelm Helling

Klaus Baalmann

Thomas Homann

Jürgen Teigeler

Frank Taetz

Heinz Hinze

Nico Wennemer

Axel Bartscher

Adam-Michael Hadamik

Stephan Frieds

Ulrich Meier

Julian König

Juergen Linnemann

Andreas Hölscher

A separator for centrifugally processing a flowable product includes a rotatable drum bounding a centrifuging chamber. The drum has a feeding and removal system having at least one feeding device and one or more removal devices composed of plastic or a plastic composite. An inner drum, composed of plastic or a plastic composite, is arranged in an outer supporting device of the drum. The feeding device and the one or more removal devices extend into the inner drum, do not rotate with the inner drum during operation, and are glued and/or welded to each other in such a way that the feeding device and the one or more removal devices are sealingly connected. The feeding and removal system has one or more grippers as the removal device, each of which one or two or more grippers has a disk segment and a shaft segment.

Separator with inner and outer drum and one or more grippers having a disk portion and a shank portion

A method for monitoring, controlling, and/or regulating the operation of a centrifuge, in particular a separator, during the centrifugal processing of a product, in particular when clarifying a product and/or when separating a product into different liquid phases. The centrifuge has a drum which can be rotated by a drive spindle, a drum mounting, and a drive motor. Force measurements are performed using one or more force sensors and analyzed, and an output is provided in the event of a deviation from a specified behavior and/or the analyses are used for or during the control and/or regulation of the operation of the centrifuge.

Method for monitoring and/or regulating the operation of a centrifuge

A method for lowering the pressure inside the hood interior of a separator arrangement with a separator with a rotatable drum includes rotating the rotatable drum about a vertical rotation axis. Before processing a product that is to be processed, a liquid is first directed through the drum and the pressure inside the hood interior is lowered, by a device, as a result of rotations of the drum in the manner of a jet pump. After the pressure inside the hood interior has been lowered sufficiently, then the actual processing of the product that is to be processed is performed.

Method for lowering the pressure inside the hood interior of a separator arrangement

A separator disk package for a rotatable drum of a centrifuge for processing of a fluid product in continuous operation is disclosed. The separator disk package includes axially stacked conical separator disks, where, between adjacent separator disks, disk gaps are respectively formed. On one or more of the axially adjacent separator disks are one or more labyrinth-like flow channels, in which, during operation, a direction of flow of a through-flowing product, which is to be clarified of solids, changes on two or more occasions through respectively at least 120&#xb0;.

Separator disk package with separator disks having labyrinth-like flow channel

A method for processing a product is disclosed. The method includes providing a separator having a rotatable centrifugal drum and a plate assembly arranged in the drum. The product is supplied into the drum. One or more of a solids phase and at least two liquid phases are separated from the product. One or more of the at least two liquid phases and the solids phase is discharged out of the drum. The supplying of the product occurs in one of a continuous and a discontinuous cyclic volume stream performed at a constant cyclic frequency where the constant cyclic frequency has a period duration which is dependent on one or more of the parameters of an inner and outer radius of a plate, an inflow stream in an intermediate space between the plate and an adjacent plate, a plate angle, and a distance of the plate to the adjacent plate.

Method for processing a product supplied in one of a continuous and a discontinuous cyclic volume stream to a separator

A solid-wall screw centrifuge includes a discharge for discharging a clarified liquid from a drum of the centrifuge. The drum includes a passage in a drum cover associated with a weir plate. The passage, drum cover, and weir plate form an overflow weir on a radial inner edge. A deflecting device is arranged on an outside on the drum cover, the deflecting device is arranged such that an exiting fluid flow from the centrifuge is one of deflected in the circumferential direction and subjected to a twist in the circumferential direction.

Fully jacketed screw centrifuge having an overflow weir

A rotatable separator drum includes a vertical rotating axis of rotation and at least one flow channel having an inlet opening and an outlet opening. Also included is at least one retaining dam arranged in the at least one flow channel in a region between the inlet opening and the outlet opening. The at least one retaining dam is configured to allow an overflow of liquid over the at least one dam and to provide for an accumulation of solids in front of the at least one dam. The at least one dam includes at least one rib arranged in a transitional region between opposing wall sections and a distributor base cover and the at least one rib includes portions having differing heights.

Separator drum having a distributor flow channel with a dam

A centrifuge includes a centrifugal drum rotatable about a vertical axis of rotation. The centrifugal drum includes one or more solids discharge orifices located at an area of the largest inside diameter of the drum. The solids discharge orifices include bores having discharge openings. The bores are arranged at least partially on an exterior of the centrifugal drum in a vertical direction Z at selected vertical heights along the exterior of the centrifugal drum.

Centrifuge including a drum and solid discharge orifices having bores arranged at selected vertical heights along an exterior of the drum

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Drensteinfurt, Germany

Kathrin Quiter