Design intent — not a specification

The concept

A pressure-reducing valve is a component that exists only to destroy energy. Vortex Core asks whether that energy can be put to work instead, and whether the result is enough to separate microplastics from the water passing through it.

How to read this page

Everything below is design intent. No part of it has been built or measured. Figures are either calculated requirements, design targets, or stated assumptions — and each one is labelled as such. Nothing here is a test result.

1. The pressure budget

The starting point is not a new energy source. It is an existing one that is currently spent on nothing.

A twenty-storey building pumps water to a roof tank. By the time that water reaches the lower floors, the column above it has produced something in the region of 80–100 PSI at the base of the riser. Domestic fixtures and fittings are rated for a fraction of that, so a pressure-reducing valve dissipates the surplus as friction and heat. It is deliberate, universal, and it wastes a genuinely useful quantity of energy.

Vortex Core replaces that valve with a tangential inlet. The water is not allowed to lose its pressure quietly — it is injected tangentially into a conical chamber at 2–5 m/s and forced into a tight spiral. Head pressure becomes rotational velocity. The device still delivers the pressure reduction the building required; it simply takes payment for it in useful work.

pressure energy in → tangential velocity → rotational acceleration (G) → particle migration → reduced pressure at outlet

Design target: 2,500–3,000 G sustained at roughly 80 PSI inlet and design flow. Whether that is reachable in a compact device is one of the questions we cannot yet answer.

Two riser schematics. On the left, labelled Today, a pressure-reducing valve destroys the surplus head pressure as heat, shown leaving the valve as wavy arrows. On the right, labelled With Vortex Core, a separation chamber spends the same pressure on rotation, and the separated fraction leaves to one side.
The whole point, in one picture. Both buildings have the same water, the same head and the same pressure to shed. The only difference is whether that pressure is destroyed by friction or spent on rotation.

2. Three stages, each using a different property

A single separator cannot resolve particles that behave in opposite ways. The concept therefore uses three stages in series, each targeting a different physical difference.

Indicative flow path. Each stage consumes a small amount of pressure (roughly 2 PSI in the concept), so the arrangement needs enough head to drive all three.

Stage 1 — heavy fraction

Water enters tangentially and forms a tight vortex. Particles denser than water — PET and PVC at 1.3–1.5 g/cm³, along with sand and sediment — are slung to the outer wall and fall through an apex valve. Design target: removal of particles above 20 µm.

Stage 2 — light fraction

The centre of a vortex is a low-pressure eye. Polymers lighter than water — polyethylene and polypropylene at 0.85–0.95 g/cm³ — migrate inward rather than outward, and can be skimmed from that core instead of being left in the product water. This is the stage with the hardest physics in it.

Stage 3 — polishing

A UV-C chamber for biological safety, and optionally a carbon block for taste and odour. This stage is conventional water treatment, included because a separator is not a disinfectant and should not be presented as one.

3. What the device would look like

A cross-section of the intended arrangement. Two things in it are easy to misread: the water changes direction, and the particles do not.

Cross-section of a hydrocyclone showing both outlets and the sorting mechanism. Feed enters tangentially at the upper left. Two radial arrows in the cylindrical section show denser particles drifting outward and buoyant particles drifting inward. Water spirals down the outer wall, reverses at the cone and climbs the core, leaving through the vortex finder at the top carrying water and the light fraction; particles denser than water continue to the apex and leave as the underflow. A note explains that the particles do not swim upstream, and that whether buoyant particles drift inward fast enough to be captured is the least certain part of the concept.
Illustration of intended behaviour — diagram v3. Particles orbit the vessel, so they sweep side to side across the section and change size as they pass nearer and further from the viewer. The two radial drift arrows are the actual sorting step. A real flow path is helical; this is a section through it, so the spiral is shown by the sweep rather than drawn as a helix. Not an engineering drawing, and not a fabrication reference.

Why the particles are not swimming upstream

A drawing like this invites an obvious objection: water only travels down, so how can anything travel up it? The answer is that the water itself changes direction, and most of it leaves by the top. In a hydrocyclone the flow splits into two co-axial vortices — an outer one descending the wall, and an inner one climbing the core to the overflow. That is what the vortex finder is for, and it is why the device has two outlets.

The particles are carried by that water. They do not push upward against the current. The separation actually happens sideways: in the centrifugal field, material denser than water drifts outward while material less dense drifts inward, and each is then transported by whichever vortex takes it. The two drift arrows on the diagram are the whole mechanism; the vertical movement is only the transport afterwards.

The flow split does have a consequence for how the thing would be plumbed in, and it is worth stating because it is easy to miss: the product water leaves by the top outlet, so it has to be piped back down the riser to reach the floors below. That is an additional run of pipe, and it is the reason this is not a like-for-like swap for a pressure-reducing valve.

The weak point, stated plainly

Radial drift is well proven for dense solids. It is far less proven for buoyant particles, which is the case this concept depends on. Three things make buoyant capture harder: the density difference driving the drift is small; the central core of a hydrocyclone is typically an air core rather than water, so a floating particle may sit at a free surface rather than being skimmed; and the argument depends on the inward drift being fast enough to reach the core before the water carrying it leaves the bottom.

That is why feasibility treats light-fraction capture as an open question rather than a design feature, and why the next step is a numerical model rather than a nicer drawing. It is also entirely possible that a hydrocyclone is simply the wrong device for buoyant material, and that this needs a different separation principle altogether. A model should be able to tell us that — and if it does, that is a useful answer, not a failure.

4. Where each stream goes

The chamber produces two streams rather than one clean and one dirty. Where they go is a separate question from how the separation works, so it is drawn separately.

Flow schematic of four stages. Stage 1 is the Vortex Core separation chamber. Its underflow, carrying the heavy fraction, runs to stage 4, the evaporation loop. Its overflow, carrying water and the light fraction, runs to stage 2, a light-fraction skimmer, whose own reject also runs to stage 4. The water then goes to stage 3, polishing, and on to the floors below. Stage 4 leaves dry plastic residue for a collection tray and recycling, and condensed water returned to the clean side.
Design intent, stage by stage. Nothing here has been built, and no stage has been tested. Note that the evaporation loop takes both reject streams — which makes it the part of the concept with the least engineering behind it.

The concept routes both reject streams — the underflow, estimated at 5–10% of total flow, plus the smaller skimmed light fraction — through a heat exchanger fed by the building’s own waste heat: chiller returns, server room exhaust, or solar gain. The water evaporates; the plastic does not. What is condensed back is clean water, and what remains is a dry residue that can be collected in a tray and sent for recycling rather than discharged as liquid waste.

Two honest caveats. First, the energy balance of this loop has not been calculated in detail; “waste” heat is not the same as available heat, and it may not be available when the loop needs to run. Second, a system that removes particles above roughly 15 µm is a pre-treatment step, not a complete potable water treatment train, and should not be described as one.

5. The physics question, stated plainly

This is the part that decides whether the concept is viable. It is also the part most easily glossed over, so here it is in full.

The rate at which a suspended particle migrates under centrifugal force follows a form of Stokes’ law:

v = (d² × |ρp − ρf| × ac) ÷ (18 × η)

where d is particle diameter, ρp and ρf are the densities of particle and fluid, ac is centrifugal acceleration, and η is viscosity. Two things follow immediately: separation gets harder as the square of particle size, and harder as the density difference shrinks.

Calculated G-force required at 50 µm and 5 µm, by polymer density. These are requirements derived from the relationship above — not measured results.
Particle size Polymer Behaviour G-force required Within our 2,500–3,000 G design point?
50 µm PET Denser than water 19 G Comfortably
50 µm Polyethylene Buoyant 147 G Comfortably
5 µm PET Denser than water 1,931 G Yes
5 µm Polyethylene Buoyant 14,679 G No — order of magnitude short
Log-log chart of the centrifugal force required to separate microplastics. The horizontal axis is particle diameter from 1 to 100 micrometres. The vertical axis is required force from 10 to 1,000,000 G. Three straight lines show PET and PVC, polypropylene, and polyethylene. A green band across the plot at 2,500 to 3,000 G marks the design point, and the shaded area above it is where the design point is not enough. PET crosses the band at 4.4 micrometres, polypropylene at 8.9, and polyethylene at 12.
The same relationship, drawn. Each line is a polymer family. Where a line sits below the green band the design point is sufficient; where it rises above, it is not. The three markers give the answer directly: 4.4 µm for PET, 8.9 µm for polypropylene, and only 12 µm for polyethylene. Below those sizes, for each polymer, particles would pass straight through. The chart is generated from the same relationship as the table above, so the two cannot drift apart.

The gap, named

At 5 µm, buoyant polymers need three to six times our design point — 8,000 G for polypropylene and 15,200 G for polyethylene. Kinetic energy scales with the square of velocity, so reaching those numbers by spinning faster is not an adjustment to the same machine; it is a different machine, with different pressures and different wear.

There is a second risk that matters as much as the first: a single chamber tuned to eject heavy PET can concentrate light polypropylene in the stream it declares clean. Any design must demonstrate that it does not simply move a problem from one species to another. How we plan to test both →

6. Where it could go

The intended deployment is one device per riser, at or near where the pressure-reducing valve already sits.

Retrofit

In an existing building, the device occupies a plant-room position adjacent to existing pressure control. No new energy supply is required, which is the single biggest practical advantage of the concept.

New build

Designed in from the start, the pressure budget, riser layout and waste-heat access can all be arranged to suit. This is where the concept is most likely to work well.

A visible installation

The chamber is a glass-and-steel object with water visible inside it. That is an opportunity but also a commitment: a public-facing installation has to work, and has to be honest about what it is doing.

Next: what we can actually prove

The concept is not the hard part. Knowing whether it is real is. Here is what exists, what does not, and the order we intend to work in.

Read the feasibility plan