UPPSALA

Technology

Two questions decide whether a high-rate clarifier performs: does the floc stay in suspension, and does the water take the path the designer intended. A deep-bed denitrification filter turns on a third: does every part of the bed see the same flow of water and air.

High-rate clarification

Keeping the floc in suspension

This applies to every configuration — plain, sand-ballasted and magnetite-ballasted alike. Two things decide it: the impeller, and the draft-tube system around it.

The impeller

We design our own blade geometry rather than fitting a general-purpose agitator. Each of the four profiles targets a specific duty, and multi-level arrangements can produce a vertical circulation pattern that acts like a draft tube without one being installed.

Mixing equipment →

Transient CFD, velocity field at 120 s. Two UPP JF-2 impellers on one shaft establish a vertical circulation loop through the full liquid depth.
Transient CFD, velocity field at 120 s. Two UPP JF-2 impellers on one shaft establish a vertical circulation loop through the full liquid depth.
Ragging on a conventional impeller.
Ragging on a conventional impeller.

Where ordinary blades fail

Municipal wastewater carries hair, fibre and textile. On a conventional blade these wrap around the hub and accumulate until the impeller stops pumping. The UPP ARH-3 swept-back hydrofoil lets that material slide outward along the blade and off the tip.

UPP ARH-3 →


The draft-tube system

The draft-tube arrangement changes what the same impeller can deliver. Two transient CFD runs of the same duty, one with a draft-tube system sized for the tank and one with a conventional arrangement, differ by 16% in flow number once both have settled.

UPPCoFlo design model: the cylinder in the flocculation zone is the UPP-Co-Tube. Its diameter, height and clearance off the floor are set for the tank, not taken from a catalogue.
UPPCoFlo design model: the cylinder in the flocculation zone is the UPP-Co-Tube. Its diameter, height and clearance off the floor are set for the tank, not taken from a catalogue.
  • Custom draft-tube system
  • Conventional draft-tube system
0.00 0.15 0.30 0.45 0.60 0.75 050100150200 steady state 0.629 0.542 +16% Physical time (s) Flow number Nq
Transient CFD. Values read after 100 s, once both cases have settled.
Data table
Time (s)Custom draft-tube systemConventional draft-tube system
00.0350.034
200.3640.300
400.3830.310
800.6250.518
1800.6290.543

Flow number Nq is dimensionless: pumped flow divided by impeller speed and the cube of impeller diameter. It measures how much liquid the impeller moves for a given size and speed, so it can be compared across cases.

What that means in the tank

Particle volume fraction for the two arrangements. With the custom draft-tube system the solids are carried up into the body of the tank; with the conventional arrangement they collect in a lower recirculating zone.

Custom draft-tube system

Custom draft-tube system — Volume fraction of particle

Conventional draft-tube system

Conventional draft-tube system — Volume fraction of particle

Volume fraction of particle

< 00.0010.0020.003> 0.004

Conditioning the hydraulics

Conventional practice assumes that taking water in at the bottom and out at the top — or the reverse — is enough to avoid short-circuiting. It is not. We build a flow-guiding arrangement for each project to stretch the real effective retention time and give the coagulant and flocculant the contact they need.

Conventional bottom-in / top-out arrangement: a large fraction of the inflow reaches the outlet well before the design retention time. Scalar shown is H₂O mass fraction from the inlet at 81 s.
Conventional bottom-in / top-out arrangement: a large fraction of the inflow reaches the outlet well before the design retention time. Scalar shown is H₂O mass fraction from the inlet at 81 s.
With a flow-guiding arrangement built for the tank: the inflow is turned back into the body of the tank instead of tracking to the outlet. Scalar shown is inlet-water volume fraction at 40.7 s.
With a flow-guiding arrangement built for the tank: the inflow is turned back into the body of the tank instead of tracking to the outlet. Scalar shown is inlet-water volume fraction at 40.7 s.

These are two separate studies, on different tank geometries and with the tracer released at different times, so they are not a controlled before-and-after of one tank. Each shows the flow pattern of its own case.

Deep-bed denitrification filtration

Every design decision in a deep-bed filter rests on one thing: whether water and air are distributed evenly across the bed. Where they are not, part of the bed is overloaded while another part does nothing, and backwash never fully recovers it. We reworked the conventional distribution arrangement.

Before

Conventional arrangement: velocity falls away along the length of the cell, so the far end is under-used.
Conventional arrangement: velocity falls away along the length of the cell, so the far end is under-used.

After

Optimised arrangement: velocity holds across the full length of the cell.
Optimised arrangement: velocity holds across the full length of the cell.

Velocity magnitude (kph)

00.2> 0.4

Process arrangement

Carbon source Coagulant / PAC Influent Rapid mix UPP-DeniFiltrera Backwash waste tank To works inlet Filtered water tank Effluent Backwash water Blower Backwash air
  1. 1 Constant level operation
  2. 2 Headloss rises
  3. 3 Air scour
  4. 4 Air + water backwash
  5. 5 Water backwash
  6. ↻ back into service

UPP-DeniFiltrera →