| FILTAN GmbH |
| Gänsgasse 9 |
| 63505 Langenselbold |
| Tel.:+49 6184 - 7081 |
| Fax:+49 6184 - 7123 |
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Datasheet
Air/ Gasfilter-Cyclone-Separator TYPE LGZFA |
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Flowrate
Vn at 10 bar: appr. 2.255 to appr. 260.241 m³/h. |
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| Removal
of solid impurities and precipitation of condensate, also
in mist form, from air or gas streams. |
| Fractional
separation efficiencies: |
| (solid
impurities) |
| 1
µm zu 98,90% |
| 3
µm zu 99,00% |
| >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: < 200mbar |
| max.
allowable pressure drop: 1,4 bar |
| Bursting
prtessure: 3 bar |
| 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. |
2nd
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
and passing along the various baffle tubes, flows through
individual tangetial jet nozzles into the lower aeparation
chamber.The flexible wall of the tangential jet nozzle provides
an automatic adjustment of the separation effect. Solid
impurities and condensate droplets are centrifuged and percipitatedin
the cyclone stage. The air or gas flowsupwards through the
smoothed zone to the coalescer cartridges arranged downstream.
Finest solid impurities, droplets of condensate and mist
of condensate are passing through the coalescer elements
from the inner tube to the outside. Solid impurities down
to sizes of one micron are retained by the filter and the
remaining condensate coalescesto large droplets. Owing to
the reduced flow rate these drops are precipitated in the
upper sepration chamber. 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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