Sized on Souders-Brown, not pipe diameter
Vessel diameter is derived from gas density at actual conditions, which is what prevents re-entrainment at the top of the element.
Filter separators, coalescers and dry gas filters removing liquid aerosols to 0.1 ppmw and solids to 0.3 µm from natural gas, hydrogen and process gas.
Overview
Liquid aerosol in a gas stream is invisible on any gauge and catastrophic in the wrong place. Sub-micron droplets pass straight through a knock-out drum, arrive at a compressor or a turbine, and remove blade material in hours.
SEPRA coalescers work in two stages. The filter medium captures and merges sub-micron droplets into large ones — this is coalescence, and it is the only mechanism that touches aerosols below 3 µm. Gravity and a vane pack then handle the enlarged droplets, which are now easy to separate.
Sizing is governed by the Souders-Brown velocity, not by pipe size. Getting this wrong is the single most common cause of coalescer re-entrainment — a filter that appears clean, at full differential pressure, and passes liquid downstream regardless. We size on gas density at actual operating conditions, every time.
Configurations
SEPRA-C
Vertical gas coalescer with two-stage element and liquid sump.
SEPRA-FS
Horizontal filter separator combining cyclone inlet, filter tubes and vane pack.
SEPRA-D
Dry gas particulate filter for solids-only duty with no liquid load.
SEPRA-H2
Hydrogen service configuration with embrittlement-resistant metallurgy and helium leak testing.
SEPRA-CA
Compressed air line filters, ISO 8573-1 Class 1 with oil-vapour carbon stage.
Vessel diameter is derived from gas density at actual conditions, which is what prevents re-entrainment at the top of the element.
Coalescing media merges sub-micron aerosols; the vane pack removes the enlarged droplets — both inside a single code-stamped envelope.
NACE MR0175 compliant metallurgy, hardness-controlled welds and PWHT where the H₂S partial pressure calls for it.
The SEPRA-H2 configuration uses embrittlement-resistant alloys and helium leak testing to 1×10⁻⁹ mbar·L/s.
Applications
Industries
Technical drawings
Vessel general arrangement
Nozzle orientation, sump volume and level-instrument positions.
Element and vane pack detail
Coalescing media stack and vane spacing.
Sizing calculation sheet
Souders-Brown derivation at design and turndown cases.
Skid P&ID
Level control, dump valve and differential pressure instrumentation.
Next step
Send flow, contaminant, rating, chemistry and available pressure. We return a configuration with the sizing basis attached.
Or call +91 79 4890 2200 · sales@worldasatech.com
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