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08 / Metal Fibre Depth Media

Sintered Metal Fibre Filter Media

A bonded, porous metal fibre network for polymer melt and process liquid filtration.

Sintered Metal Fibre Filter Media
Representative product. Final construction follows the approved specification.

Application and Selection.

Sintered fibres form a permeable structure with space for retained contaminants. Select retention, permeability and structural backing for the finished filter.

Media families
A3 · C4 · C3 · D4 · E4 · B3 · F3
Sheet size
Listed catalogue size: 1500 × 1180 mm
Construction
Pleatable or non pleatable, by media family

Permeability and bubble point comparisons require matching test conditions. Confirm the airflow unit, test pressure and media construction.

Technical Information

Open a section to view the details, tables and illustrations.

Construction & Family Selection

A Fibre Network with Space for Contaminants

In graded depth media, coarser inlet regions intercept larger contaminants while finer regions retain smaller material within the structure. Distributing retention through the depth helps use the available pore volume.

Product photograph or dimensional drawing — Sintered Metal FibreProduct photograph or dimensional drawing — Sintered Metal Fibre

Fibre close up and explanatory depth filtration schematic

Family

Construction

Catalogue Positioning

A3

Multilayer; pleatable

Polymerisation and spinning

C4

Multilayer; pleatable

Compression resistance and dirt capacity

C3

Multilayer; pleatable

Monomers and lower - viscosity fluids

D4

Multilayer; non - pleatable

High strength polymer leaf discs

E4

Symmetrical multilayer

Improved pleating behaviour

B3

Single layer; pleatable

Low viscosity, low - contamination liquids

F3

Single layer; pleatable

Economical, lightweight media

Listed sheet size: 1500 × 1180 mm. Protective mesh is offered on one or both sides.

Match the Construction

The diagram illustrates a graded medium. Confirm the actual layer sequence, flow direction, protective mesh and structural backing for the selected family.

A3 - Polymerisation & Spinning

Multilayer Media for Pleated Filters

A3 is the broad pleatable family in the catalogue, covering polymerisation, spinning and process liquid applications.

Model

AVG. BUBBLE POINT Pa

Porosity %

AIR PERMEABILITY* L/(dm²·min)

3A3

12300

67

10

5A3

7600

80

34

7A3

5045

74

62

10A3

3700

78

108

15A3

2470

80

180

20A3

1850

82

265

25A3

1480

79

325

30A3

1235

79

450

40A3

925

76

620

60A3

630

86

1350

75A3

480

84

1470

80A3

450

85

1510

90A3

410

88

1740

100A3

360

89

2020

* Confirm units, test conditions and acceptance tolerances; see “Understanding the Test Data”.

Specify the Finished Filter

Confirm the media thickness, steel grade, supporting layers and effective filtration area before choosing a finished candle or pack assembly. A media code alone does not define the complete filter.

Retention Requirement

Request the particle size, removal efficiency and test method associated with the selected model. The numerical prefix in a model name is not presented here as an absolute micron rating.

C4 & C3 - Depth Filtration Media

Select for the Fluid and Mechanical Duty

C4 - Compression Resistant Media

Multilayer, pleatable construction aimed at dirt capacity and compression resistance.

Model

AVG. BUBBLE POINT Pa

Porosity %

AIR PERMEABILITY* L/(dm²·min)

5C4

7400

73

32

7C4

5100

73

54

10C4

3700

73

75

15C4

2400

73

180

20C4

1850

73

230

25C4

1500

73

294

C3 - Lower Viscosity Fluids

Multilayer, pleatable media for monomers, prepolymers and other lower viscosity fluids.

Model

AVG. BUBBLE POINT Pa

Porosity %

AIR PERMEABILITY* L/(dm²·min)

5C3

7100

86

37

10C3

3500

85

110

15C3

2400

85

203

20C3

1700

86

345

25C3

1700

86

385

30C3

1230

86

650

40C3

1036

86

675

* Confirm units, test conditions and acceptance tolerances; see “Understanding the Test Data”. The source lists 1700 Pa for both 20C3 and 25C3; these entries are retained as published.

Mechanical Duty

Bubble point pressure is a wetting test result. It is not the allowable operating pressure or the collapse differential pressure of the completed element.

D4 & E4 - Disc and Pleated Media

Choose the Required Forming Behaviour

D4 - High Strength Disc Media

Multilayer media for polymer leaf disc filtration; specified as non pleatable.

Model

AVERAGE BUBBLE POINT Pa

Porosity %

AIR PERMEABILITY* L/(dm²·min)

2D4

18000

51

3

3D4

12300

72

13

5D4

7700

72

24

7D4

5000

72

43

10D4

4020

72

53

12D4

3200

72

85

15D4

2410

72

135

20D4

1900

72

165

25D4

1480

71

260

30D4

1230

75

350

40D4

925

75

625

E4 - Media for Pleating

Symmetrical multilayer construction developed for improved pleat formation.

Model

AVERAGE BUBBLE POINT Pa

Porosity %

AIR PERMEABILITY* L/(dm²·min)

3E4

11500

70

10

5E4

8000

81

36

7E4

5300

68

40

10E4

3700

74

75

15E4

2466

71

132

20E4

1850

71

220

*Confirm units, test conditions and acceptance tolerances; see “Understanding the Test Data”.

B3 & F3 - Single Layer Media

Options for Different Service Priorities

B3 - Low Contamination Liquids

Pleatable media for lower viscosity liquids such as hydraulic oil and fuel.

Model

AVERAGE BUBBLE POINT Pa

Porosity %

AIR PERMEABILITY* L/(dm²·min)

5B3

7000

79

45

10B3

3700

81

125

15B3

2470

78

250

20B3

1850

80

400

40B3

925

84

1100

60B3

530

74

1660

F3 — Economical Media

Lightweight, pleatable construction positioned as an economical option.

Model

AVERAGE BUBBLE POINT Pa

Porosity %

AIR PERMEABILITY* L/(dm²·min)

10F3

3500

71

90

15F3

2600

77

140

20F3

1800

70

240

40F3

925

71

625

60F3

550

71

1200

* Confirm units, test conditions and acceptance tolerances; see “Understanding the Test Data”.

Product photograph or dimensional drawing — Sintered Metal Fibre

Representative sheet surface and edge detail

Understanding the Test Data

Compare Values on a Defined Test Basis

Average Bubble Point Pressure. This is the label used in the catalogue. In a wet bubble point test, gas displaces the wetting liquid from pores. The result depends on the liquid and procedure; establish the defined endpoint before comparing suppliers.

Porosity. Porosity is the fraction of void space in the medium. It differs from particle removal efficiency, woven mesh open area and the effective area of a pleated filter.

Air Permeability. The catalogue reports a flow per unit area. A meaningful comparison requires the test pressure difference, gas conditions and specimen construction. These conditions must be confirmed for the selected media

Unit Clarification

The catalogue prints the airflow unit as “I/dm².min”. This guide interprets it as L/(dm²·min), meaning litres per square decimetre per minute. Confirm the unit and test pressure with the supplier.

What the Tables Do Not Define

The page does not provide complete grade specific thicknesses, alloy specifications, retention efficiency curves or finished element pressure and temperature limits. Obtain these for the selected construction before approval.

From Media Data to Process Performance

Pressure loss depends on fluid viscosity, flow, filtration area and media resistance. Airflow figures cannot directly predict polymer melt pressure loss.

Use application specific flow data and include the support structure and element geometry in the review.

Controlled Comparison

Compare candidate media at the same fluid, temperature, throughput and required retention. Verify clean pressure loss and subsequent pressure rise in the actual supported element.

Application, Cleaning & Validation

Qualify the Media in the Operating Process

Metal fibre media are used in polymer candle, leaf disc and spin pack filters. Removing solids, agglomerates and gels can support filament continuity and film quality; actual performance depends on the contamination and selected medium.

Define the Process. Record polymer or fluid grade, viscosity basis, flow range and temperature. Identify contamination type, current element reference and the reason for replacement or improvement.

Review the Assembly. Provide a drawing with active area, media stack, supports, flow direction, seals and end connections. Include operating pressure, change out differential pressure and transient conditions.

Set Trial Acceptance. Record initial pressure loss, pressure rise per operating hour or tonne, run duration and product quality. In spinning, include spinneret blockage and filament break trends; in film, track the agreed defect measure.

Cleaning and Reuse

Select the cleaning method for the deposit, alloy and assembled filter. Polymer filters may require thermal, chemical or ultrasonic treatment, followed by cleanliness and integrity assessment. Use a qualified procedure matched to the element

Compare post cleaning flow and integrity results with a documented new element baseline. Integrity testing and particle removal efficiency measure different things; an acceptance method needs validation for the particular medium and element design.

RELEASE FOR REUSE Set approved acceptance limits, retain the element identification and cleaning history, and inspect the support structure, joints and sealing surfaces before returning the filter to service.

Release for Reuse

Set approved acceptance limits, retain the element identification and cleaning history, and inspect the support structure, joints and sealing surfaces before returning the filter to service.

Supply Information

Specify the model, alloy, thickness, dimensions, mesh protection, final element drawing, quantity, required documentation and trial approval criteria. Include expected annual consumption and the requested delivery schedule.

Prepare Your Enquiry

What to Send Us.

Media family or existing reference; polymer or liquid; temperature; throughput; retention target; flow resistance test basis; support layers.

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Application Focused Support

The Right Solution Starts
with Your Process.

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