Powderflight General Brochure - metric0 pages

TYPICAL DIMENSIONS
A
B
C*
D
E
F
H
J

M75
76
365
x150
175
250
200
800
180

M100
102
485
x 200
200
330
260
900
220

M160
168
650
x 250
250
460
350
900
360

POWDERFLIGHT
CONVEYING SYSTEMS

* Multiples of

CONVEYOR CAPACITIES

SWEPT VOLUME: LITRES/MIN

During conveying, powders are subjected to turbulence and aeration,
which in effect reduce their bulk density. Since we recommend no
more than 50% to 60% loading by volume, a realistic output can be
estimated by multiplying the swept volume given in the table, by the
bulk density and dividing by 4. This will be a conservative figure
which may well be exceeded in practice.

TEST FACILITY
All models of Powderflight Conveyors are available for tests with
customers’ materials at our test facility at Glossop.

R.P.M.
90
150
190
240

M75
330
540
680
870

M100
730
1190
1500
1900

M160
2500
4200
5300
N/A

e.g. Talc at 0.8 kg/litre :
M100 at 190 rpm output :
1500 x 0.8 = 300 kg/min
4
(This figure has been exceeded by 30% on test.)

OTHER PRODUCTS FROM THE UNITRAK POWDERFLIGHT RANGE

‘TipTrak’ bucket elevator

‘Bagstander’ FIBC Discharge
System

‘Screwfeeder’ with agitated
in-feed hopper

Dinting Lane Industrial Estate, Glossop, Derbyshire SK13 7NU, UK
Tel: +44 (0)1457 865038 Fax: +44 (0)1457 869776 Email: info@unitrak.co.uk Web site: www.unitrak.co.uk

High Output
with Versatility
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•
•
•
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Dust-tight conveying.
High output relative to power and cost.
Minimum headroom required at discharge.
No separation of blended products.
Minimum attrition of fragile particles.
No filtration necessary at discharge.
Low noise level.
Any angle of operation.