Alpha alumina
Porous support and microfiltration layers. Rigidity and mechanical resistance.
Cross-flow filtration engineering for extreme pH, hot streams and demanding cleaning. MF, UF and NF modules and plants using high-performance ceramic materials.

A porous inorganic structure supports the selective layer inside the channels. The feed flows tangentially; permeate passes through the wall and the retained fraction becomes concentrated.
We combine support, selective layer and geometry to achieve the separation. The range extends from particles to small molecules, with ceramic nanofiltration down to 200 Da nominal MWCO.
Porous support and microfiltration layers. Rigidity and mechanical resistance.
Selective ultrafiltration layers for macromolecule separation.
MF, UF and NF layers. Selectivity extending to the subnanometre scale.
MF and UF layers, with options for fine separation and chemical resistance.
Minimum nominal molecular-weight cut-off in the range.
Particles and suspensions
Colloids and macromolecules
Smaller solutes
NF references include TiO₂ layers rated at 0.9 nm / 450 Da and 1.0 nm / 750 Da. MWCO describes a nominal molecular-weight cut-off; retention of each compound is determined using the actual feed.
Selection ranges within the portfolio. Material, cut-off and geometry are specified in the datasheet of the proposed membrane.
Ceramic stability is valuable where chemistry, heat or membrane regeneration constrain production.
A system designed for the operating temperature can retain heat and simplify conditioning stages.
We select the membrane material for acidic or alkaline media, or compatible solvents, together with the seals and housing.
Cross-flow sweeping, backwashing and intensive CIP support permeability recovery.
| Design constraint | Cross-flow ceramic filtration | Polymeric membrane |
|---|---|---|
| Temperature and chemistry | A broad selection of inorganic materials for demanding service. | Operating window determined by the polymer and module. |
| Intensive cleaning | Greater scope to restore performance under demanding cleaning protocols. | Concentration, oxidants and temperature kept within the specified limits. |
| Element stability | Rigid support and ceramic selective layer. | Fibres, sheets or tubes with properties specific to each material. |
| Economic criteria | Durability, availability and resource recovery. | Attractive capital cost and compactness under compatible conditions. |
pH, temperature and pressure limits are specified for the complete membrane, gasket and module assembly. They are selected together for continuous service and cleaning.
We define retention and the destination of each stream: recovering water, preserving useful components or concentrating the fraction requiring management.
Protein fractionation, clarification and component recovery using the appropriate cut-off.
Separation of retainable soil in acidic or alkaline cleaning solutions.
Filtration at process temperature in an assembly designed for the duty.
Treatment of acidic or alkaline media, or solvents compatible with the selected materials.
Separation of the dispersed phase in machining, washing and process waters.
Reduction of turbidity and retainable colour and organic fractions.
Clarification and concentration in mineral-loaded circuits; MF options for abrasive media.
Clarification of beer, wine and other food streams by cross-flow filtration.
Ceramic NF for selective separation of small organic compounds and certain dissolved ions.
Technology is selected according to the target product. Ceramics stand out when fractionation must be combined with process temperature and intensive cleaning.
Neptuno designs the membrane system and its balances to recover components, produce usable permeate and reduce the volume sent downstream.
A process selection, not a mandatory sequence. We combine stages according to composition, temperature and target permeate and concentrate quality.

We define a cross-flow unit suited to your feed and operating regime. The scope can be an integration module, a skid or a plant with its own CIP circuit.
In streams where temperature, chemistry or demanding cleaning affect production continuity. The inorganic structure expands separation and regeneration options, with benefits for availability, service life and resource recovery.
It is the minimum nominal molecular-weight cut-off in the ceramic NF range. It enables small-molecule separation applications beyond the scope of MF and UF. We select the membrane and verify retention and flux for the compound of interest.
Yes. MF and UF support clarification and fractionation, including protein concentration. For lactose or other small solutes, we assess NF; where the objective is water removal and stream concentration, we assess RO. Ceramics add value through their hot-processing capability and cleanability.
CIP solutions, process components and heat from hot streams. We define what should remain in each fraction to reduce resource losses and the volume requiring management.
Both. Neptuno can specify and supply integration modules, manufacture a skid or develop a cross-flow filtration plant with recirculation, instrumentation, automation and CIP. We coordinate materials, interfaces and documentation with your engineering team.
We start with operating and cleaning conditions and select the ceramic layer, support, seals and housing together. This turns material resistance into a defined plant capability, with an operating specification established for the project.
Send us your flow rate, water analysis and treatment objective.
We will review equipment selection, integration and the data needed to size your project. You can attach your water analysis or P&ID to your email.
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