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Projects and Engineered Systems completed by Filtration Technology

Projects

Select from the list below
Auto Poly Prep System and Dosing
Eltham WTP Upgrade
Matarangi Beach Estates
Te Aroha WTP Upgrade
Trojan UV - Hamilton
Waikouaiti Membrane Filtration Upgrade
West Taieri Membrane Filtration Upgrade

Te Aroha WTP Upgrade

Background
Over the past couple of years there has been an increase in the consumption often drawn from the Te Aroha Water Treatment Plant. Concurrently Inghams Chicken Poultry Processing Plant, on the Hauraki Plans, have increased their business significantly and now require additional water. As a consequence MPDC has undertaken to supply Inghams with potable water. This has resulted in the Te Aroha Water Treatment Plant being upgraded and capacity increased from 4000 to 8000m3 /day.
The project was funded by MPDC with a significant contribution from Inghams Chickens.
The upgrade had to be carried out while the plant remained in operation, and in fact during the latter part of the project increased production was required.
The process selection for the upgrade involved;

  • Changing the coagulant from Aluminium Sulphate to Poly Aluminium
  • Chloride doubling the number of filters and then automation
  • Retrofitting Tube Settlers to the two existing
    Clarifiers
  • Upgrading chemical storage and dosing
  • Installation of Turbidity Meters


The plant maintenance and operations provider is Kaimai Valley Services (KVS). Work was
allotted with civil and building components being contracted to KVS with Filtration Technology carrying out the mechanical and plant controls.

Change of Coagulant
The raw water is supplied from up to five sources that are blended in a balance tank that then discharges to the treatment plant. Of the source three are gravity fed, low turbidity, low alkalinity streams, whilst the other two are pumped, one of which is the Waihau River. Gravity sources are the preferred supplies. With such varied raw water sources, we determined that Poly Aluminium Chloride would produce a faster forming floc and have less dependence on raw water alkalinity. A further advantage of the Poly Aluminium Chloride is its greater tolerance to changes in raw water. By changing the coagulant the plant capacity increased.

Filters/Automation
The existing filters were very much in an ‘as built’ condition, largely unchanged since construction in 1967. Their control had been modified however, with discharge flow controlling the filtered water valve. The filter inlet channel water depth controlled the plant inlet flow.
To relieve production pressure, two epoxy coated steel filters constructed and installed adjacent to the existing plant. Although round these filters have the same surface area and operation depth as the original filters.
A new control system was installed on all the filters with ultrasound level sensors adjusting the filter outlet valves to maintain a constant filter water level. Backwashes are initiated when the level begins to rise. Raw Water Mag Flow Meter now has direct control of the raw water inlet valve. There is a secondary pressure sensor in the filter inlet channel as a failsafe to plant flooding.

Retrofitting Clarifiers with Tube Settlers
By installing Tube Settlers into a Clarifier the rise rate can be doubled from typically 2m3 /m 2 /hr to 4.5m3 /m 2 /hr. We have thereby been able to double the clarifier’s capacity without needing to add civil structures. This has shown good cost saving on alternative options. Installed the Tube Settlers have required some changes in the way the plant is operated. There is no longer a clarified water blanket for the operator to visually inspect and desludging cones are no longer used. Jar test, sludge index test and clarified water turbidity have become chief operating tools.

Upgrading of Chemical Storage and Dosing
With the increased water production, the chemical storage and dosing systems were too small. In order to make plant operation easier, larger storage vessels for Chlorine and LiquiPAC have been installed. Dosing Pumps have been re-sized.

Installation of Turbidity Meters
To meet requirements of both DWSNZ and contract supply, online turbidity monitoring has been added to all filter output.


Specification

Previous Plant Capacity

4000m 3 /day

Upgraded Plant Capacity
8000m 3 /day
Required Treated Water Quality
DWSNZ2000/2005
Filters
Quantity
2 (new) / 2 (existing)
Material of Construction
Epoxy Coated Steel
Dimensions
4100mm dia x 4400mm high
Filter Floor Plate
4090mm dia x 10mm thick
Internal Weir
840mm OD
Filtration Area
12.64m2
Filtration Rate
6.6m3 /m2 /hr (4 duty filters)
Filtration Rate During B/Wash
8.8m 3 /m 2 /hr (3 duty filters)
Filter Nozzles
Make
Altek KSH
Model
C1
Quantity
196/Filter
Slot Width
0.2mm
Filter Media  
Type
Sand
Effective Size
0.6-1.2mm
Depth
600mm
Backwash
Type
Separate Air Scour/Wash
Control
Ultrasonic Operation on Headloss
Control Valves
Air Actuated Keystone
Tube Settlers
Make
Brentwood
Model
AccuPac 6000 Series
Pack Depth
600mm (IFR-6024)
Surface Area
43.6 m 2 (per Clarifier)
Effective Surface Area
41.6m 2 (per Clarifier)
Effective Rise Rate 4.1m 3 /m 2 /hr @ plant flow 333m 3 /m 2 /hr
Equipment
Dosing Pumps
Wallace and Tiernan
Turbidity
Hach 1720E
Chlorination
Wallace and Tiernan
Analysers
Wallace and Tiernan
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