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Metal Super Raschig Ring Structure & Pressure Drop Explained

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Metal Super Raschig Ring Structure & Pressure Drop Explained

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Metal Super Raschig Ring Structure & Pressure Drop Explained
October 10, 2026

 

 

Stainless steel metal super Raschig rings with sinusoidal web structure stacked for distillation column random packing

Figure 1: Metal super Raschig rings in SS316L — sinusoidal webs form multiple liquid films and maintain high open area.

Metal Super Raschig Ring Structure & Pressure Drop Explained

Engineer's Brief: A metal super Raschig ring is a high-performance random packing built from a thin-walled cylinder with alternating sinusoidal webs instead of plain walls. The wave webs create several thin liquid films, promote interface renewal, and keep free volume at 96–98%. Compared with a plain metal Raschig ring it avoids nesting; compared with standard metal Pall rings it typically gives lower pressure drop at equal throughput and higher flooding capacity in retrofits. FXSINO supplies super raschig-style rings in carbon steel, SS304/304L and SS316L/316L.

1. Geometry: Why the Sinusoidal Web Matters

A plain Raschig ring is a hollow tube with height equal to outside diameter. It is cheap and chemically simple, but wall flow and channeling are severe, and packing factor is high. A super Raschig ring replaces the straight wall with curved/sinusoidal strips and reconnects them at repeated contact points. The result:

  • • Multiple films: Sinusoidal webs split the liquid into several thin films; recurrent contact points remix the films and renew the gas-liquid interface.[4](@ref)
  • • High open area: Free volume 96–98% depending on size, so gas passes with little contraction and dry ΔP stays low.[5](@ref)
  • • Anti-nesting: Alternating wave frequency/amplitude reduces entanglement during dumping and makes removal easier.[4](@ref)
  • • Low bulk weight: Thin stamped sheet gives high surface area per unit mass; support grid load is lower than ceramic and often lower than solid-wall metal rings.[4](@ref)
  • • Fouling tolerance: Open structure suits liquids with minor solids; fewer dead zones than closed-window geometries in dirty service.[5](@ref)
Macro photo of single metal super Raschig ring showing sinusoidal side webs, contact points and thin stamped wall

Figure 2: Web detail — sinusoidal strips and welded contact points create turbulent film surfaces while keeping the core open.

2. Standard Size & Geometric Data

FXSINO quotes super raschig-style metal rings in common metric sizes. The table below mixes metric project sizes with reference values from metal super-ring bulletins; treat as selection reference, not certified hydraulic guarantee.[4,5,13](@ref)

Metric size (mm) Approx. SR no.* Surface area (m²/m³) Free volume (%) Bulk density SS (kg/m³) Pieces/m³
25 0.3 (close) 180–220 95–96 210–340 45,000–180,000
38 0.5–0.7 130–180 96–97 185–275 16,000–45,500
50 0.7–1 100–150 97–98 165–220 9,500–32,000
76 2–3 70–100 98 150–165 4,300–9,500

*SR no. is an approximate cross-reference to published metal super-ring bulletins (0.3/0.5/0.7/1/2/3). Metric 25/38/50/76 is not strictly equivalent to any single SR number; confirm tooling with FXSINO. Bulk density varies with wall thickness, steel grade and waveform.[4,13](@ref)

3. Pressure Drop: Dry, Wet & Loading

Pressure drop of a random bed depends on gas capacity factor F (= u·ρv0.5), liquid load L (m³/m²·h), packing size, tower diameter and irrigated wetted area. For super raschig metal rings the practical trend is:

  • Dry ΔP: Very open geometry — published metal super-ring dry pressure drop is already lower than a 50mm metal Pall ring at the same F-factor.[4](@ref)
  • Wet ΔP at low L: Air/water tests on No.0.3–0.5 sizes show dry ΔP around 20Pa/m at zero liquid and roughly 50–80Pa/m at L=1–2m³/m²h in small-column references; values scale with size, F-factor and tower diameter.[1](@ref)
  • Wet ΔP at high L: Gap vs Pall grows with liquid load because films and windows stay open; super-ring wet ΔP can be substantially below comparable high-performance rings.[4](@ref)
  • Loading/flooding: In 50mm-class comparisons, super raschig flooding capacity was about 25–33% higher than 50mm Pall and 10–15% higher than some high-performance rings; exact margin depends on system and distributor quality.[2](@ref)
  • Vs plain Raschig: Plain metal Raschig has much higher packing factor and channeling; super raschig is not a fair 1:1 swap — re-rate bed height, support open area and distributor density.
Pressure drop chart of metal super Raschig ring vs metal Pall ring showing lower slope under air-water irrigation

Figure 3: Reference ΔP vs gas capacity — super raschig slope stays below standard Pall as liquid load increases (illustrative, replace with FXSINO test curve).

4. Super Raschig vs Metal Pall vs Plain Raschig

Item (50mm class) Plain metal Raschig Metal Pall ring Metal super Raschig
Wall structure Solid cylinder Cylinder + side windows + inner tabs Cylinder + sinusoidal webs/contact points
Free volume ~65–70% ~90–94% 97–98%
Dry/wet ΔP Highest Low Very low (lower than Pall in refs)[2,4](@ref)
Flooding capacity Lowest High Higher than 50mm Pall (+25–33% in refs)[2](@ref)
Efficiency / HETP Poor (channeling) Good all-round Good; up to ~14% better separation than 50mm Pall in ammonia/water refs[4](@ref)
Mechanical / dirty service Robust, but poor hydraulics Windows can deform under high dP/load Web structure stable; open for solids-bearing liquid[8,5](@ref)
Use case Legacy/ceramic acid only General distillation/absorption High-capacity retrofit, vacuum, low ΔP, dirty absorbent

Pall comparison figures are from ammonia-air/water and cyclohexane/n-heptane references; do not apply generic "% reductions" to every fluid without system data.[2,15](@ref)

5. Material Selection

Material Key limit Typical service
Carbon steel Non-corrosive, dry/hydrocarbon; temp by code Atmospheric distillation, hydrocarbon absorption
SS304/304L Low chloride; general organics Solvent recovery, mild aqueous absorption
SS316L Chloride/weak acid better than 304 Chlorinated scrubbing, pharma, acidic absorbent
SS410 / alloy High temp/strength or special corrosion High-pressure retrofits, sour/erosive service

6. Sizing Rules & Tower Internals

  • Size vs diameter: Keep nominal size ≤ D/30 for even distribution; 50mm for 1.5m ID, 76mm for ≥2.3m, 25–38mm only in small/high-efficiency columns.
  • Support open area: Use a camel hump support grid or punched support plate with ≥80% open area; super raschig low ΔP is wasted if the support restricts flow.
  • Distributor density: Small 25mm needs more drip points/m² than 76mm; pair with a liquid distributor/redistributor for beds >6m.
  • Hold-down: Light stamped metal at high F or vacuum needs a bed limiter/hold-down plate; size bar gap to retained element, not to nominal OD.
  • Entrainment: For high gas velocity add a wire mesh demister above the top bed.
Metal super Raschig rings loaded in stainless distillation column with support grid and liquid distributor during installation

Figure 4: Super raschig charge with support grid and distributor — for low ΔP distillation or absorption retrofit.

7. Application Guide

  • • Vacuum distillation: Low ΔP per stage protects vacuum system; 50–76mm super raschig or structured packing depending on HETP target.
  • • Atmospheric distillation/refinery: High flooding capacity supports debottleneck without larger shell.
  • • Absorption/scrubbing: SO2, HCl, NH3, CO2 — open web handles variable liquid load; 316L for corrosive scrub liquor.
  • • Stripping/regeneration: Steam stripping of VOC or amine regeneration where low ΔP reduces reboiler/compressor cost.
  • • Dirty/once-through liquors: Super raschig open structure tolerates fines better than small-window Pall; still less tolerant than hollow-ball media.

8. Quick FAQ

Q: How much lower is pressure drop than a metal Pall ring?

A: Published 50mm-class tests report super raschig wet ΔP roughly 60% lower than Pall in one cyclohexane/n-heptane dataset and clearly lower than Pall under air/water at equal F; ammonia/water retrofits show smaller ΔP reductions at equal throughput (e.g., No.1 vs 1.5" Pall about −21 to −33%). Always re-run with your fluid properties.[2,15](@ref)

Q: Can I replace plain Raschig or Pall 1:1 by volume?

A: No. Super raschig has higher free volume and different HETP, so 1:1 volume usually over-designs or changes separation duty. Send existing bed height, throughput, pressure budget and HETP; FXSINO proposes size, bed height and internals as a package.

Q: Is super raschig better than structured packing for vacuum?

A: Structured packing gives the lowest ΔP/HETP in clean vacuum service; super raschig is preferable when you need random-packing flexibility, dirty feed, easy reload, or retrofit inside an existing support/distributor layout. For deepest vacuum and tight HETP, compare both with wire mesh structured packing.

Get a Metal Super Raschig Quote

FXSINO is a manufacturer of metal random packing & tower internals — super raschig rings, metal Pall rings, support grids, distributors and demisters. Custom sizes in carbon steel/SS304/316L, fabricated to drawing, shipped worldwide.

Send tower ID, service fluid, pressure, temperature, gas/liquid rates, target HETP or ΔP budget. We return size recommendation, bulk volume, support open area, distributor density and a same-day budget quote. FXSINO supplies the full package — support grids, bed limiters, redistributors and demisters.

Contact FXSINO: jackieqiu9202@gmail.com | +86 18507999558

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