Kloeckner-humboldt-deutz Ag

Albert Suessegger

Siegfried Strasser

Albrecht Wolter

Frank Fischer-Helwig

An energy-saving effective sifter used in interparticle crushing of brittle charging stock such as cement clinker in the nip of a high pressure roller press including a dynamic sifter having a rotating rod basket and laterally preceding the rotary rod basket sifter by a fluidized bed pre-sifting chamber having an admission opening at the top with a chamber defined between opposed porous walls to provide a pre-sifting zone with the walls formed by angularly adjustable baffles in one form, and passing air across the zone toward the rotary rod basket, removing a coarse grain fraction below the pre-sifting chamber, removing a medium grain fraction from beneath the rotary rod basket and removing fine material axially of the rotary rod basket passing the medium grain and coarse grain fraction into an interparticle crushing high pressure roller press having a nip pressure in excess of 2 t/cm of roller length, mixing the medium grain fraction and coarse grain fraction with a pre-comminuted pulverulent material such as cement clinker, passing the discharge of the interparticle crushing roller press to a deagglomerator and feeding the deagglomerated material into the sifted. In one form, the fine material rod basket is passed through a dust removal cyclone with the discharge of the cyclone and the medium grain discharge of the rod basket being passed to a tube mill.

Sifter for sifting granular material and grinding system with insertion

A rotary sifter for separating different fractions of particulate material having a cylindrical outer housing and three rotary cages with vertical bars through which material and air pass inwardly with the cages independently rotary mounted, and channels communicating with the spaces below the rotors for collecting the separate fractions of separated material, and additional air delivery means to each of the channels which collect the separated fractions.

Sifter

A separator for separating fractions of granular material particularly for use in an interparticle crushing product bed comminution press including an outer conically shaped chamber with means for receiving air and the product to be comminuted at the lower end of the chamber, an inner conical chamber, a second coarse grits outlet leading from the inner conical chamber, a first coarse grits outlet leading from the outer conical chamber, a rotor at the upper end of the inner conical chamber having turbo elements thereon, baffles surrounding the turbo elements, and a fine products discharge from the upper end of the inner chamber with the coarse grits discharge from the outer chamber led back to the inlet of a high pressure interparticle crushing roller mill and the fine grits material discharged from the inner chamber led to a tubular mill.

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Bergisch Gladbach, Germany

Albert Suessegger