Low-pressure membrane barrier that removes colloids, bacteria and suspended solids ahead of RO or NF, quantified by membrane area, TMP and flux condition.
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Granular-bed filtration that removes suspended solids ahead of a membrane, sized here from design flow, filtration rate and bed geometry.
Granular-bed filtration that removes suspended solids ahead of a membrane, sized here from design flow, filtration rate and bed geometry.
Separation mechanism and feed window. Handles raw waters carrying suspended solids, colloids and organic colour. It is a barrier for particle load, not for dissolved salt, and it is not a disinfection step.
What the process produces. A filtered stream at the design filtration rate. Filtrate quality is not a design output here; turbidity and SDI are site test results.
Energy. Gravity-driven. Head loss across the bed is the energy consideration.
Where this technology normally sits in a treatment train. The steps either side of it are documented in the Library as separate entries.
The parameters an engineer actually sets, and why each one drives the design. EngiMetric does not assume any of them.
| Parameter | Why it matters |
|---|---|
| Design flow | Sets the required filter area. |
| Filtration rate | The primary area driver; higher rates mean more area or more units. |
| Bed depth and effective size | Determines media volume and the head-loss profile. |
| Filtrate recovery | Sets how much flow reaches the next stage and therefore its duty. |
Industry maturity and commercial status describe the technology itself. EngiMetric support and quantitative modeling describe what this platform does with it — and those two are read from the engineering registry at build time, so they cannot drift from the code.
Every tool below exists and is live. EngiMetric does not duplicate a formula here — the calculation lives in the tool, and this page links to it.
Available as a configured treatment-train step with a stated net filtrate recovery. Its filtrate flow sets the duty of every downstream stage.
Configurable in the Plant Designer as an ordered treatment-train step. Its duty, mass balance and equipment requirements are computed from the inputs you state, not assumed.
EngiMetric does not publish a bibliography of external literature for catalogued technologies. Where a figure is required, it is entered by the engineer from a datasheet or a published reference, and it is labelled as an input.