Separation-apparatus

1. A separation-apparatus for separating from a particle-stream at least a first fraction with particles of a first group of dimensions, and a second fraction with particles of a second group of dimensions, comprising:

an infeed-device for the particle-stream, wherein the particle-stream is a moist stream of particles sized in the range of 0-15 mm,

a rotatable drum having at its circumference plates, each plate having a radially extending hitting surface for the particles,

at least a first receiving area proximal to the drum for receipt therein of particles of the first fraction, and

at least a second receiving area distant from the drum for receipt therein of particles of the second fraction,

wherein the infeed-device comprises a vibrating plate having an edge positioned above the drum, which edge is embodied as an outlet for the particle-stream, the infeed-device further comprising a slide-plate immediately adjacent to said edge that tilts downwards as seen from the edge, the slide-plate being inclined at an angle in the range 70-90 deg. with respect to the horizon, the vibrating plate and the slide plate cooperating to cause in use a mono-layer type flow of the particle stream comprising a plurality of particles across a width of the particle stream, and the edge of the vibrating plate being positioned vertically or near-vertically above an axis of rotation of said drum so as to cause that in use the particles of the particle-stream fall towards the drum in a direction aimed towards said axis of rotation or its immediate vicinity, and such that the plates of the drum impinge on said falling particles at a moment that said plates are in a vertically or near- vertically upwards oriented position extending from the drum.

2. The separation-apparatus according to claim 1 , further comprising the rotatable drum being configured so that in use the drum rotates at a speed causing that the plates impinge on the particles with a horizontal speed in the range 20-30 m/s.

3. The separation-apparatus according to claim 1 , further comprising the infeed-device being configured to operate in use at a vibrating-frequency of more than 10 Hz and an amplitude of less than 5 mm.

4. The separation-apparatus according to claim 1 , further comprising the apparatus having a housing configured to protect the particles from outside weather-conditions.

5. The separation-apparatus according to claim 1 , further comprising the plates comprising a backing that slopes from the free extremities of said plates towards the drum's circumference so as to counter turbulence behind said plates.

6. The separation-apparatus according to claim 1 , further comprising means for providing a gas flow having a flow-direction that is pointed from the second receiving area towards the drum.

7. The separation-apparatus according to claim 1 , further comprising said at least second receiving area distant from the drum comprising a conveyor for discharging the particles of the second fraction received in said second area, at which conveyor's outlet a blower is provided supplying a downwardly directed airflow for removal of particles of the first fraction that stick to particles of the second fraction.

8. A method of separating a moist stream of particles sized in the range 0-15 mm in a separation-apparatus according to claim 1 .

9. The method according to claim 8 , wherein the particles are separated into at least a first fraction with particles having dimensions in the range of 0-2 mm, and a second fraction with particles having dimensions in the range of 2-15 mm.

10. The method according to claim 9 , further comprising the particle stream originating from waste-incineration ashes, and wherein the separation-apparatus is used to classify metals from said ashes into the said first fraction and said second fraction.

11. The method according to claim 10 , further comprising processing said second fraction in a dry-separation method to separate the metals into ferrous and non-ferrous metals.

12. The method according to claim 8 , further comprising the stream of particles having a moisture-content of 15-20 percent by weight.

13. The method according to claim 8 , further comprising prior to subjecting the particle stream by the processing in said separation-apparatus, the particle stream is sieved so as to restrict the particles to sizes in the range 0-15 mm.

14. The separation-apparatus according to claim 1 , wherein the angle of departure, α, of the particles at the plates in operation is less than 12 degrees relative to the horizon.