Device and method for sorting a particulate stream
The invention relates to a device for continuously sorting a particulate stream, comprising: a) a conveyor ( 1 ) for conveying the particulate stream to a separation device, b) a sieve ( 7 ) for separating the particulate stream according to size, characterized in that it further comprises c) a per-sieve ( 3 ) comprising elongated sieve openings located between the convey or outlet and the sieve d) and a mechanical impact device for providing mechanical impacts to the pre-sieve ( 3 ). The pre-sieve allows to separate elongated objects like threads or wires form the particulate stream which would otherwise clog or block subsequent separation devices including the sieve.
1. Device for continuously sorting a particulate stream, comprising:
a) a conveyor ( 1 ) for conveying the particulate stream to a separation device,
b) a sieve ( 7 ) for separating the particulate stream according to size,
c) a pre-sieve ( 3 ) comprising elongated sieve openings formed by fingers extending towards an end portion of the pre-sieve with the tips of the fingers not being connected in that end portion, wherein the pre-sieve is located between an outlet of the conveyor and an inlet of the sieve, and wherein a portion of the particulate stream passes through the elongated sieve openings to the inlet of the sieve; and
d) a mechanical impact device for providing mechanical impacts to the pre-sieve ( 3 ).
2. Device according to claim 1 , characterized in that the pre-sieve ( 3 ) comprises elongated sieve openings including an angle of −40° to 40° with the conveying direction of the conveyor.
3. Device according to claim 1 , characterized in that the conveyor is a screw conveyor ( 1 ).
4. Device according to claim 3 , characterized in that the pre-sieve ( 3 ) encloses part of the circumference of the screw conveyor in an axial end portion of the screw conveyor.
5. Device according to claim 4 , characterized in that the radial distance between the conveyor screw ( 1 ) and the pre-sieve ( 3 ) is less than 10% of the conveyor screw diameter.
6. Device according to claim 5 , characterized in that the radial distance between the conveyor screw ( 1 ) and the pre-sieve ( 3 ) is less than 5% of the conveyor screw diameter.
7. Device according to claim 1 , characterized in that the width of the elongate openings increases from the base to the tip of the fingers.
8. Device according to claim 7 , characterized in that the increase in width is by a factor of 2 to 6.
9. Device according to claim 8 , characterized in that the increase in width is by a factor of 3 to 5.
10. Device according to claim 1 , comprising at least one of:
a) the width of the elongate openings at the base is between 1 and 5 mm;
b) the width of the elongate openings at the tip of the fingers is between 4 and 20 mm;
c) the length of the fingers from base to tip is between 100 and 500 mm;
d) the mesh size of the sieve ( 7 ) is between 200 and 1,000 μm.
11. Device according to claim 10 , comprising at least one of:
a) the width of the elongate openings at the base is between 2 and 4 mm;
b) the width of the elongate openings at the tip of the fingers is between 10 and 14 mm;
c) the length of the fingers from base to tip is between 150 and 250 mm; and
d) the mesh size of the sieve ( 7 ) is between 300 and 800 μm.
12. Device according to claim 1 , characterized in that the mechanical impact device is a hammer or piston-vibrator.
13. Device according to claim 1 , characterized in that the impacting force and impacting frequency of the mechanical impact device is controllable.
14. Device according to claim 1 , characterized in that the mechanical impact device provides impacts in the area of the base of the fingers of the pre-sieve ( 3 ).
15. The use of a device of claim 1 for the separation of a particulate ash stream from a fluidized bed boiler.
16. A method for operating a fluidized bed boiler, comprising the steps of:
a) carrying out a fluidized bed combustion process;
b) removing at least one ash stream from the fluidized bed boiler;
c) separating the ash stream into at least two fractions, wherein the separation includes a separation step using the device according to claim 1 ;
d) recirculating a separated particle fraction into the bed of the fluidized bed boiler.
17. The method of claim 16 , characterized in that the boiler is a circulating fluidized bed boiler (CFB) or a bubbling fluidized bed boiler (BFB).
18. The method of claim 16 , characterized in that the fluidized bed and the ash stream from the fluidized bed comprise ilmenite particles and that the separated recirculated particle fraction is enriched in ilmenite.
19. The method of claim 15 , characterized in that the separation includes a step of using a magnetic separator ( 12 ) comprising a field strength of 2,000 Gauss or more.
20. The method of 16 , characterized in that the field strength is 4,500 Gauss or more.
21. The method of claim 18 , characterized in that the fraction of ilmenite in the bed material is 25 wt. % or more.
22. The method of claim 21 , characterized in that the fraction of ilmenite in the bed material is 30 wt. % or more.