Abstract: A drive technology for vehicle treatment installations. The drive technology comprises a washing installation drive motor (2) for a vehicle treatment system (69). The washing installation drive motor (2) is preferably configured as a synchronous motor, in particular as a brushless DC motor. The drive motor (2) has an internal rotor (3) with a hollow shaft (5). As an alternative, or in addition, the washing installation drive motor (2) is configured as a modular drive unit (7). The modular drive unit (7) has a uniform configuration and is provided and configured for driving different apparatus constituent parts of a washing installation. The drive technology further includes a washing installation drive (1), a treatment element (52, 55, 57, 64) and also a vehicle treatment system (60) with a corresponding washing installation drive motor (2), and an associated operating method.

Abstract: The hydrophilic organic contaminants and hydrogen peroxide present in semiconductor fabrication reclaims are removed by means of adsorption of a pyrolysate of a macroreticular sulphonated vinyl-aromatic polymer having a carbon content of at least 85% by weight and a carbon/hydrogen atomic ratio of from 1.5:1 to 20:1. In spite of their hydrophobic surface, the pyrolysates have a comparatively high adsorptivity for these contaminants and provide for distinctively higher removal rates than customary activated carbons.

Abstract: In order to clean a deposit filter having filter elements (4) installed in a suspended manner, first, with the plenum (3) filled with flushing medium, the liquid is discharged completely or partially from the filter chamber by way of an emptying line (7) by opening a ventilating line (6) arranged in the uppermost region of the filter chamber (2), then, by means of a pressure-generating line (8) which is arranged on the plenum and by way of which propellent gas or flushing medium under pressure is conveyed into the plenum, a pressure surge is generated in the plenum and drives the flushing medium through the filter elements, and finally the impurities, together with the liquid, are discharged. Before the pressure surge is exerted, an underpressure can be generated in the filter chamber, in order further to increase the effect. If desired, the filter elements (4) can have an upper gas-impermeable region (5).

Abstract: For the conditioning of ion exchange resins, pure water is recirculated over a bed of the resin to be purified or of the resins to be purified. The pure water has a residual salt content of less than 50 ppb and a content of free acids or free bases of less than 5,000 ppb. The organic and inorganic substances washed out of the resin or the resins are removed continuously from the circulating water by methods for the purification of water. The process can be used for conditioning the ion exchange resins used in an ultra pure water production system.

Abstract: An apparatus for the continuous electrochemical desalination of aqueous solutions includes a wound module having a central electrode, around which are wound an anion exchanger membrane and a cation exchanger membrane, and an outer counterelectrode. Each membrane is sealed at an inner edge thereof and at a outer edge by a respective clamping device, or are anchored in a synthetic resin block, in such a way that a dilution chamber and a concentrate chamber are defined. The dilution chamber and/or the concentrate chamber may contain an ion exchanger resin. The central electrode and the outer counterelectrode each may have a constriction over at least a part of the circumference thereof. The central electrode may furthermore have a recess for receiving the inner clamping device or the inner synthetic resin block in order to achieve a winding having as spiral a cross section as possible.