There are many types of filter cartridges and bags; if you are not sure of what you require, the first step is often determining if you require depth or surface filtration. Each method serves a specific purpose based on particle concentration and fluid characteristics.
Surface Filtration implies that particles are retained mostly on the surface of the media, forming a layer of material that increases the efficiency or fineness of particles retained. Generally speaking, this type of filter media is referred to as having a "nominal retention". It may initially be 60% to 70% efficient at retaining the targeted particle size, but as the "cake layer" develops, it can eventually become nearly 100% efficient.
Nominally rated media is the most common and is less expensive than depth media. The amount of surface area directly correlates to the solids loading capability and related pressure drop. Examples include perforated strainer baskets, mesh woven strainer baskets, and both monofilament and multifilament style filter bags.
Surface filtration works best when the particle percentage is <200 PPM and the particles themselves are non-deforming. Gelatinous particles may extrude through the openings as the differential pressure increases. The volume of particles which can be retained corresponds directly to the total surface area of the filtration media. The efficiency can be either nominal (applicable to woven filter bags) or absolute (applicable to rigid media such as defined pore, perforation and mesh lined designs).
Depth Filtration refers to a thicker media or multiple layers of media, forming a torturous path to retain particles. This engineered media ideally retains larger particles towards the surface and progressively finer particles through the thickness or layers. High-performance designs are often rated at 95% to 99% efficiency and are not reliant on a filter cake for their performance. Depth filtration media can handle a higher concentration of particulates compared to surface filtration media across a specific span of time.
Needlefelt filter bags begin with polyester or polypropylene fibers compressed into rolls of high-density sheets. This material is then punctured with barbed needles, producing a pore structure with tangles of fibers that provide a non-direct "torturous path". Fluid entrained with particles follow the path of least resistance with finer particles caught deeper in the pores and larger particles closer to the surface. As the pores become clogged, the denser areas of the media retain particles until the system reaches its maximum recommended differential pressure (typically 20 – 30 PSI).
Meltblown fibers are manufactured by atomizing raw polymers with hot air. These fibers can be engineered for size and density by controlling the ratio of the polymer flow rate and pressure against the temperature of the atomizing air. Absolute rated depth filtration filter bags are created from multiple meltblown layers to form an ever-increasing density, allowing for stratification of retained particles throughout the thickness of the filter bag. Some designs feature as many as 7 distinct layers of density.
Fiber Migration: This refers to the potential for the fibers making up the filter bag to break loose and go downstream. To prevent this in needlefelt material, the external surface is typically "singed" – heated to bond the fibers together. The meltblown process naturally bonds fibers together, making downstream migration negligible.
Layered Depth Stratification
Nominally rated needlefelt designs are the least expensive and provide a minimal amount of depth filtration. Meltblown filter media will cost more due to the complexity of its multiple layers of density and thickness enabling it to hold more particles.
Return on Investment (ROI): While depth media costs more, it typically lasts significantly longer. Your ROI calculation must include:
Absolute rated efficiency is often expressed as a **BETA Ratio**. For more technical details, refer to our article Filter Bag Design.
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