Match the structure
Use Cylinder area for screens or sleeves; use Pleated cartridge only when media folds radially between outer and inner diameters.
Engineering Tool · Filter Elements
Additional tools: Pleated area & pleat count | Parallel cartridge count
Calculate cylindrical or pleated filter area, then estimate face velocity or required active area from operating flow.
Quick definition: a plain cylinder uses exact geometric area; a pleated cartridge uses a theoretical media-area approximation and must be confirmed against the actual pleat profile and finished element.
Choose the calculation that matches the element construction.
Geometric results for a plain circular cylinder.
Lateral area = π × diameter × lengthEngineering Tool · Flow & Area
Calculate superficial velocity from actual operating flow and active filtration area, or estimate the total active area needed for a chosen design velocity.
Use the flow at the filter's operating pressure and temperature.
Superficial velocity based on total active area.
v = Q ÷ AQ in m³/s, A in m², v in m/s. The area is the total usable filter media area, not open-pore area.
No. This is superficial velocity: volumetric flow divided by the total active filtration area. Local pore velocities depend on porosity and flow distribution.
Use actual volumetric flow at operating conditions. Convert standard or normal flow to actual flow first with the Standard to Actual Gas Flow Calculator.
Select it using media specifications, fluid properties, particulate loading, allowable pressure drop and process testing. The prefilled 0.02 m/s is an arithmetic example, not a recommended design limit.
Not necessarily. Bonded edges, blocked folds, seams and end caps reduce usable area. Verify it against the finished element before using the required-area result for purchasing.
Use Cylinder area for screens or sleeves; use Pleated cartridge only when media folds radially between outer and inner diameters.
Exclude end-cap bonding zones, gasket coverage and blocked sections from the active pleated length.
Confirm theoretical area with the actual pleat profile, spacing, seam allowance and approved manufacturing drawing.
Plain cylinder: lateral area equals πDL. Adding two circular ends gives πDL + πD²/2, but filter sleeves and open-ended elements normally use only lateral active area.
Pleated cartridge: approximate media area equals 2 × pleat depth × pleat count × effective length, where pleat depth is estimated as (OD − ID)/2.
The pleated formula treats each pleat side as a flat rectangle. It does not add curved fold radii, overlap, seam allowance, adhesive penetration or media blocked by end caps.
More theoretical media area does not automatically mean more usable flow. Tight pleat spacing can cause contact, poor cleaning and uneven flow distribution.
| Element type | Area basis | Typical use | Main limitation |
|---|---|---|---|
| Plain cylindrical screen | πDL | Protective screen or filter sleeve | Does not include ends |
| Closed solid cylinder | πDL + πD²/2 | Geometric surface estimate | Ends may not be active media |
| Radial pleated cartridge | 2NhL | Approximate media area | Assumes flat pleat faces |
| Finished filter element | Verified drawing or measured media | Final specification | Requires real construction data |
The lateral surface area is π multiplied by diameter and length. Total geometric area adds the two circular ends.
Usually no. Bonded or solid end caps do not pass fluid, so active filter area normally includes only exposed media.
A practical preliminary estimate is two pleat faces multiplied by pleat depth, pleat count and effective filter length.
Fold radius, media thickness, seam overlap, end-cap embedment, tapered pleats and spacing change the real developed area.
Not by itself. Flow also depends on media permeability, pore structure, viscosity, pressure drop, contamination loading and support layers.
The calculator divides the optional target area by estimated area per element and rounds the result upward. Hydraulic and housing checks are still required.
Share your dimensions, media, pleat construction, flow conditions and drawing with our engineers.
Engineering disclaimer: Use the geometric estimate to compare element layouts. Confirm seams, sealed ends, blocked folds and other inactive zones on the finished drawing before recording active area. Review flow capacity with the actual medium, operating conditions and relevant test data.
Calculate one face's usable area for a circular disc, annular ring or rectangle after excluding known sealed borders. Sum exposed pieces in parallel; do not multiply layers stacked in series.
Disc: gross = πD²/4; usable = π(D − 2b)²/4. Ring: gross = π(D² − d²)/4; usable = π[(D − 2b)² − (d + 2c)²]/4. Rectangle: gross = WL; usable = (W − 2b)(L − 2b). D = outside diameter; d = inner diameter; b = outside sealed width; c = inside sealed width. All lengths use one unit; results are converted to m².
Sealed area = gross − usable. Parallel area = usable per piece × parallel quantity. Minimum parallel pieces to reach a specified target = ceil(target / usable per piece). This assumes one exposed face and identical active pieces. Do not multiply bonded layers sharing the same flow path or assume that face area proves flow, pressure-drop or filtration rating.
No. Layers in series generally share the same projected face area. Only independently exposed parallel surfaces are summed.
Use the actual sealed, welded or masked regions on the approved drawing. This tool does not infer them from material grade or mesh count.
Use the face velocity section with actual operating flow and a separately established design basis. Area alone does not prove flow capacity.
Use the active filter area with the volumetric flow appropriate to the task. Liquid permeate flux is commonly reported as LMH (L/m²/h). For gases, use actual operating flow for superficial face velocity; flow stated at standard or normal conditions must be converted before physical sizing.
Liquid LMH: J = Q × 1,000 / A when Q is m³/h, giving L/m²/h. The equivalent superficial speed is J ÷ 3,600,000 m/s. Actual gas: face velocity = Qactual /(3,600 A) for Q in m³/h. Reference-state gas: Qreference/A in reference m³/m²/h reports a normalized throughput only; it is not an actual operating velocity and cannot substitute for Qactual/A.
If a supplier quotes Nm³/h or Sm³/h, record the reference temperature and absolute pressure, then convert using the Standard to Actual Gas Flow Calculator. Enter the converted actual flow here under the Gas: actual flow setting. Differences in reference states or gas compressibility matter.
10 m³/h actual liquid flow through 0.5 m² active media area gives 20,000 LMH. This is an arithmetic example, not a recommended industrial filter operating flux. A gas rate of 100 actual m³/h across 0.5 m² corresponds to 0.05556 m/s superficial face velocity. Neither result predicts clean/dirty pressure drop, cake accumulation, retention efficiency or service life.
No. 1 LMH is one litre per square metre per hour, so it equals 1/60 L/min/m².
No. Normal or standard gas volumes refer to a specified reference pressure and temperature. Convert to actual operating volumetric flow first.
No. Open-area geometry, media permeability, fluid viscosity, pressure differential and fouling must be considered separately.
Calculate media area from a measured developed width, or estimate it with an ideal triangular pleat profile. Supports metal pleated cartridges and sintered felt pleated elements.
Measured: A = net developed width × active axial length. Ideal profile: developed width = 2N√(depth² + (pitch/2)²). Count estimate: N = floor(πD / requested pitch); achieved pitch = πD/N. Exposed area = A × entered exposure fraction.
Use the unfolded length along the corrugated cross-section for developed width. Exclude axial bonded ends and the circumferential seam overlap before entry. Area counts one media sheet, not two faces and not multiple support layers. Enter 100% if no additional known obstruction applies. The exposure fraction is supplied by you; it is not a universal correction. Triangular geometry ignores bend radii, thickness, compression and variable pitch. Count estimates require a defined reference circumference and manufacturing review.
Measured net media dimensions give geometric area. The exposed-area result only applies your known obstruction allowance. Flow distribution, blocked valleys and service loading can reduce working area further.
No. Crowding, contact between pleats and limited flow access can offset extra media area. This tool does not predict pressure drop or validate manufacturability.
Enter the diameter of the circumference where your pitch was defined. Outer and inner diameters give different pitches; do not mix those references.
Examples are arithmetic demonstrations, not recommended factory specifications. Unit reference: NIST — 1 inch = 25.4 mm exactly.
Estimate the number of cartridges online from actual volumetric flow, a selected media face velocity and the exposed media area of one cartridge.
Required area = actual flow / (3600 × selected media face velocity). Online cartridges = ceil(required area / area per cartridge). Installed total = online + offline spares. Area-based average velocity = actual flow / (3600 × online area).
Enter a velocity selected from a suitable validated design or test; the tool supplies no recommended velocity. Use exposed media area, not cartridge cross-section. All online cartridges are assumed identical and equally loaded. Offline spares do not contribute active area. Gas flow must be actual volume at operating pressure and temperature, not Nm³/h or standard flow. Housing distribution, pressure drop, fouling, cleaning and redundancy design require separate assessment.
No. It is an area-based count estimate. Flow distribution, connections, available pressure and dirty-element resistance need independent checks.
Only when they are online and carrying flow. Offline spare cartridges are shown in the installed total but excluded from active area.
Convert normal or standard gas flow to actual volumetric flow at the operating conditions first. This tool does not perform that conversion.
Examples are arithmetic demonstrations, not recommended factory specifications. Unit reference: NIST — 1 inch = 25.4 mm exactly.
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