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Anderson / Separator Vessels / Vane Separators / Inline Vane Separator

Inline Vane Separator

AVS · AVS-24 as modeled — 8″ 150# RF, carbon steel

Liquid-laden gas enters the inlet, drops its bulk liquid on the box baffle and spreads through the wet plenum. A full-bore sealed bundle casing leaves it only one way out — through the pocket-type vane bundle, where the stream is forced to change direction several times. The gas negotiates the turns; the heavier liquid cannot, and impinges on the wetted vane walls. It coalesces, converts to sheet flow and runs into the shielded vane pockets, isolated from the gas stream, then drains by gravity into the sump.

Drag to orbit, scroll to zoom. Cutaway and the part key isolate individual parts; Play walkthrough steps the principle of operation one stage at a time.

LIVE 3D SECTION

How it works

 

The mixture enters the 8″ inlet and strikes the box baffle, which drops bulk liquid out of the stream before it reaches the vanes. The sealed bundle casing closes the vessel across its full bore, so the gas has no path to the outlet except through the vane bundle.

 

Passing the bundle, the stream is forced to change direction several times. Low-density gas negotiates the path; high-density liquid cannot turn with it. At each turn a centrifugal force throws liquid particles onto the wetted vane wall, where they coalesce, absorb further droplets and convert to sheet flow.

 

Sheet flow travels into the vane pockets. Once inside, the liquid is isolated from the gas stream and protected from re-entrainment. The pockets discharge to the drain pan and troughs, then fall by gravity to the sump below, where collected liquid pools in the liquid-sealed sump and discharges through the 2″ drain. Clean gas crosses the dry plenum and leaves the 8″ outlet.

 

Pocket vane against hook-type vane

 

  • Shielded pocket. Collection and drainage are uninterrupted and protected from re-entrainment, so each vane handles a higher liquid volume.

  • Lower pressure drop. More capacity than hook-type vanes for the same duty.

  • More laminar flow. An advanced flow profile keeps turbulence down through the bundle.

  • Smaller bundle. Less vane area for the same application, which means a smaller, more economical vessel.

 

Separation performance and the inlet coalescer

 

Efficiency falls as droplet size decreases. To separate below the vane threshold the bundle must be preceded by a coalescer — either a hookless vane bundle in the inlet nozzle, or the stainless wire mesh pad on the vane face shown in the model — which grows incoming droplets to a size the vanes can remove.

 

The wire mesh pad merges fine mist into droplets large enough for the vanes to catch, which is what carries removal from the plain-bundle threshold down to 3 microns. Without a coalescing stage the bundle works on the droplet population it is given.

 

Sizing

 

Vane separators are sized to the duty, not selected from a size list. Vessel diameter, bundle face area and nozzle sizes follow from flow rate, operating pressure, gas and liquid densities and inlet loading. Supply those with the connection schedule and required code stamp; the arrangement shown in the model — AVS-24 with skirt and drain — is a representative build of that arrangement.

 

Typical service

 

  • Gas transmission and gathering. Liquid knockout in the line ahead of meters, compressors and regulators.

  • Compressor protection. Taking entrained liquid out of the suction stream so it does not reach the machine.

  • Steam service. Removing condensate carried with the steam ahead of turbines, traps and process users.

  • Compressed air. Water and oil carryover removal downstream of aftercoolers and receivers.

  • Fine mist duty. Applications that need a coalescing stage ahead of the vanes to bring droplet size up to what the bundle can capture.

DIMENSIONAL DATA — AS MODELED

Shell OD × wall

24 in × 1/4 in

 

Tangent to tangent

60 in

 

Heads

2:1 elliptical, 6 in deep

 

Overall height

96 in incl. skirt

 

Skirt

24 in, base ring + 8 anchors

 

Inlet / outlet

8 in 150# RF

 

Inlet CL / outlet CL

55 in / 55 in

 

Drain

2 in 150# RF

 

Vane bundle

14 × 10 × 26 in

 

Vane pitch

1 in, 5 passes

MATERIALS OF CONSTRUCTION

Shell & heads

SA-516 Gr 70 steel

 

Skirt

SA-36 steel

 

Nozzles / flanges

SA-106 B / SA-105

 

Vane bundle

SA-240 316 SS

 

Bundle casing

SA-240 316 SS

 

Coalescer pad

316 SS wire mesh

 

Gaskets

Non-asbestos fiber

 

Fasteners

SA-193 B7 / SA-194 2H

 

Finish

Industrial gray enamel

SEPARATION PERFORMANCE

0–110% design flow

100% ≥ 8 Âµm

 

At design flow

100% ≥ 5 Âµm

 

With inlet coalescer

100% ≥ 3 Âµm

Request sizing · RFQ

Additional Vane and Separator Arrangements

Vertical vessel carrying an Anderson vane pack for bulk gas–liquid separation.

View product

Pocket-type vane assemblies across the steam space of a boiler drum.

View product

Centrifugal element followed by a coalescing mesh pad in one vessel.

View product

Parallel cyclone tubes for high throughput in a compact vessel.

View product
Steam turbine rotor close-up

Sizing is set by the duty, not the catalog.

Vessel diameter, bundle face area and nozzle sizes follow from flow rate, operating pressure, gas and liquid densities and inlet loading. Send us the conditions and the connection schedule and we will size it.

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