| FILTAN GmbH |
| Gänsgasse 9 |
| 63505 Langenselbold |
| Tel.: +49 6184 - 7081 |
| Fax:+ 49 6184 - 7123 |
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Datasheet
Air/ Gasfilter-Cyclonseparator TYPE LGFA-H |
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Flowrate
Vn at 10 bar: appr. 7.498 to appr. 105.443 m³/h. |
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| Removal
of solid and liquid impurities from air or gas streams. |
| Fractional
separation efficiencies: |
| (solid
impurities) |
1
µm zu 98,90% |
3
µm zu 99,90% |
| >5
µm zu 99,99% |
| (liquid
impurities) ) |
1
µm zu 98,60% |
3
µm zu 98,90% |
| >5
µm zu 99,97% |
| pressure
drop under clean conditions: < 100mbar |
| max.
allowable pressure drop: 1,4 bar |
| Bursting
prtessure: 3 bar (cartridges of the 2nd stage) |
| Boiler
plate, grain refined or austenitic steel, shell depending
on requirements. Boiler plate and grain-refined shell are
sandblasting inside and outside acc. to SA 21/2, finished
inside with two layers of benzene-resistant coating, outside
with one layer. Fittings are of 1.4514 Silumin or cadmium-plated
steel. |
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| Two
stage cyclone-separator with coalescer-elements |
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| The
vessels are manufactured and inspected acc to the German AD-Merkblatt
by an independant inspection agency. Pressue vessel calculation
to teh ASME code on requirement. |
| 1st
stage: The
fine filter cartridges provides a surface action and
are of a folded star construction, made of high quality
cellulose which is impregnated with phenolic resin for
an incresed stability. Aöternatvily there are special
materials on disposal. |
2ndt
stage: The coalescer cartridges are made of impregnated
cellulose and glass fibre providing a combined surface and
deep action and performs the following two functions:
| a)
Removal of solid impurities down to 1 micron. |
b) Coalescence
of the fine condensate droplets to larger ones and their precipitation.
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| The
air or gas stream enters the vessel through the inlet nozzle.
Major quantities of the impurities are precipitated in the
lower separation chamber. Solid impurities down to sizes of
one micron are retained by the filter elements in the 1st
stage. Finest solid impurities, droplets of condensate and
mist of condensate are flowing to the 2nd stage of the vessel
passing through the coalescer elements from the inner tube
to the outside. The remaining condensate coalesces to small
droplets and are flowing down into the collecting chamber
2nd stage. The purified air or natural gas is leaving the
vessel through the outlet nozzle. |
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| Additionals: |
| Quick opening
closure, 100% x-raying, pressure vessel calculation acc. to ASME
and other various accessories can be ordered. |
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