2. We are providers of innovative
engineering solutions for water within
Industry.
Our Services include:
» Design and Implementation
» Multi-disciplined Services
» Energy Management
» Consultancy
SureWaters: Water resource management

3. What we can introduce today:
‘Unique Treatment Process’
Reduce operational costs
Eliminate chemicals
Re-use in house
Potentially valuable By-product

4.  Process
 Hygiene
 Cooling
 Heating
 Domestic use
All leading to effluent

5. Water is a vital resource..........
 On average, 6 litres of water is consumed
per kilo of production
 Incoming mains on average is £1.00 per M³
 Effluent outfall is between £1.50 and £4.00
per M3
 Over the last ten years these costs have
almost doubled and are still rising

6. Industrial:
 Chemical coagulation and DAF plants
 Chemicals added to coagulate and remove contamination
 Sand and particulate filters
 Coarse mechanical filters to remove large particles
 Municipal and occasionally industrial:
 Anaerobic digestion plants
 Tanks with aerobic microbes to “consume” contaminants
 Aerobic digestion plants
 Tanks with anaerobic microbes to “consume” contaminants

7. These methods allowed.......
 Rain and “grey” water could be used for toilet flushing
Then potentially:
 Cleaning up waste water for lorry wash
 Cleaning up waste water for Cooling and boiler feed waters

8. BUT
Just what is really possible?
Apart from:
 Toilet flush
 Lorry wash
 Boiler make up
We can then add:
 Wash water in low care areas
 Wash water in high care areas
 Chiller water
 Evaporative condensers
Then the really big winner?
Potable water recovery

9. How

10. What are the characteristics?
• Low capital cost
• No chemicals
• Not pH dependent
• Low running costs
• Small foot print
• Fast rate of pollutant removal
• Concentrated and shear resistant
pollutant ‘float’
• Operational simplicity

11. • Electrocoagulation is an electrochemical method of treating
polluted water; whereby sacrificial electrodes corrode at
the anode face and release an active coagulant, causing
pollutants to cluster together into semi-solids.
• This is accompanied by gas release on the cathode face of
the electrodes; which integrates into the growing pollutant
clusters, causing them to become buoyant.
• Pollutant removal can occur by ‘coagulation only’ which
causes pollutants to sink or by ‘coagulation and flotation’
which causes pollutants to float.

13. An electrocoagulation reactor comprises sacrificial electrodes
(Aluminium or Iron) that:
• dose the polluted water with a coagulating agent of
metal cations (positively charged ions e.g. Aluminium
Al3+).
• produce electrolytic gas bubbles into the flow
(Hydrogen).
The process can be characterised by:
• Fast rate of pollutant removal,
• Highly concentrated and shear resistant pollutant ‘float’,
• Compact size,
• Operational simplicity,
• Relatively low capital and very low operational costs.

14. Current density directly influences:
 Coagulation dosage,
 Hydrogen bubble generation rate,
 Hydrogen bubble size,
 Fluid mixing and mass transfer at the sacrificial electrodes.
SureWaters’ on-site demonstrations and trials equate the
amount of coagulant / bubbles delivered versus the mass of
pollutants that require to be removed.

16. STAGE 1
Backwash tank
Sludge Tank 30m3
15m3 working
3mD x 5.2H
55m³ inflow 2.5D x4H
Parabolic screen Gross solids
60m³ 40ft container
EC container – 40ft
10 core EC
60m3 per hour clarifier
Plant
Particulate filter
2 x 65m3
Re pressure tank
duty duty
30m3 – 3mD x 5.2H
250m3 tank EC balance tank
Clarifier – 7L x 3.5Wx2.5H
7.8D x 6H 15m3 2.5D x4H
STAGE 3 STAGE 2
2 x20ft container
Joined 2 x 40ft container 2 x40ft container
25% Joined Joined
50% RO 3 wash water
wash water 4.5m3 Ultra – filtration and
Wash water from RO1 RO 1 Ultra violet
30m3 30m3
RO4
4.5m3
Ultra – filtration and
50% Wash water from RO2 RO2
Ultra violet
re-use water 30m3
30m3
UV polish 75%
re-use water
Water for re-use Concentrate to ST
or off site

18. Trial results
Sample Description FOG TSS COD Sample Description FOG TSS COD
24-Oct Raw Pre Daf 133 300 2500 25-Oct Raw Pre Daf 1550 2640 5750
Al5683 10A 45 270 2700 Al6082T6 10A* Post DAF 60 140 1250
% Removal 66.2% 10.0% -8.0% % Removal 96.1% 94.7% 78.3%
24-Oct Raw Pre Daf 1530 2490 7400 25-Oct Raw Pre Daf 1550 2640 5750
Al5683 20A 65 190 1500 Al6082T6 10A Pre DAF 60 235 2250
% Removal 95.8% 92.4% 79.7% % Removal 96.1% 91.1% 60.9%
24-Oct Raw Pre Daf 1530 2490 7400 25-Oct Raw Pre Daf 1550 2640 5750
Al5683 30A 240 355 1400 Al6082T6 20A Pre DAF 74 200 2500
% Removal 84.3% 85.7% 81.1% % Removal 95.2% 92.4% 56.5%
24-Oct Raw Pre Daf 1530 2490 7400 25-Oct Raw Pre Daf 1550 2640 5750
Al5683 10A 100 115 950 Al6082T6 30A Pre DAF 20 295 3500
% Removal 93.5% 95.4% 87.2% % Removal 98.7% 88.8% 39.1%
26-Oct Raw Post Daf 1810 2860 7650
Stainless Steel 415 785 4050
% Removal 77.1% 72.6% 47.1%

20. Current
Water usage: 38176 over last 7 months - 7.5m3/hr average with
peaks during night.
(Site estimate 14/10/10)
COD – 2500mg/l
SS – 1000mg/l
(Site estimate 14/10/10)
Mogden:
Using Scottish Water standard calculator
Current Annual Cost - £99,128

21. Future with SureWaters
Stage 1
Volume – 38176 over last 7 months - 7.5m3/hr average with peaks during night.
COD at 84% - 1200mg/l
SS at 92% - 190mg/l
Therefore costs:
EC Treated Annual Cost - £49,859
Effluent Savings per annum - £49,269
Chemical Savings per annum - £30,000 (Site estimate 14/10/10)
The chemical free sludge should now allow for this to be removed from site at no
cost
Sludge Savings per annum - £224,000 (Site estimate 14/10/10)

22. Future with SureWaters
Stages 2 and 3
65% recycle
Effluent Saving (After Stage 1 implementation)– £32,525
Incomer Volume Charge Saving - £42,539
Total Further Saving - £75,064

23. Stage 1
Equipment, delivery, installation (Mechanical and Electrical) and commissioning.
£112,289.00 for a 2 core 10m3/hr system capital excluding VAT
(17 month payback using parameters shown above, 4 months if sludge is taken into
account)
£140,248.00 for a 3 core 15m3/hr system capital excluding VAT
(21 month payback using parameters shown above, 6 months if sludge is taken into
account)
Stages 2 and 3
£235,280.00 total for a 2 core 10m3/hr system plus 65% recycle excluding VAT
(18 month payback using parameters shown above, 7 months if sludge is taken into
account)
£278,792.00 total for a 3 core 15m3/hr system) plus 65% recycle excluding VAT
(22 month payback using parameters shown above, 9 months if sludge is taken into
account)

24. Contaminants TSS COD
(ppm)
Raw Influent 279 3,766
Processed 6 9.7
Reduction 97.9% 99.75%

25. Just what is possible?
Ready meals food production
Original
Incomer - £1.00/m3
Effluent loading- £2.56/m3
Effluent volume - £0.44/m3
Cost per annum - £670,000
Treated Recycled
Incomer - £1.00/m3 Incomer £1.00/m3
Effluent loading - £0.33/m3 Effluent loading - £0.00
Effluent volume - £0.44/m3 Effluent volume - £0.44/m3
Cost per annum – £275,000 Cost per annum - £60,000
Saving - £395,000 per annum Saving - £610,000 per annum
ROI – 11 months ROI – 9 months

26. Just what is possible?
Fresh fish preparation
Original
Incomer - £1.10/m3
Effluent loading- £3.18/m3
Effluent volume - £0.46/m3
Cost per annum - £840,000
Treated
Incomer - £1.10/m3 Sale of recovered fish oils
Effluent loading - £0.29/m3 300 tonnes per annum
Effluent volume - £0.46/m3 £500 - £1,200 per tonne
Cost per annum – £188,000
Saving - £652,000 per annum £155,000 to £360,000 INCOME
ROI – 7 months

27. Just what is possible?
24 hour food production
Original
Incomer - £0.90/m3
Effluent loading- £2.58/m3
Effluent volume - £0.38/m3
Cost per annum - £2,828,000
Treated Recycled
Incomer - £0.90/m3 Incomer £1.00/m3
Effluent loading - £1.10/m3 Effluent loading - £0.00
Effluent volume - £0.38/m3 Effluent volume - £0.44/m3
Cost per annum – £1,350,000 Cost per annum - £350,000
Saving - £1,478,000 per annum Saving - £2,478,000 per annum
ROI – 11 months ROI – 10 months

28. The following data was calculated and agreed by the client
following an extensive on site demonstration (operating the
mobile unit @ 5 m3 / hour):
» Projected power consumption ~ £2.55 per 50m³ treated.
» Coagulation consumables – EC sacrificial electrodes
˃8 lots of 4 plates every three to four weeks;
˃Approximately 832 plates per annum projected;
˃£3,744 per annum.
There are NO further EC
operating costs

29. Applying some of these techniques to your
water during the manufacturing process will:
» Reduce operational costs
» Eliminate use of chemicals
» Reuse water within your manufacturing
process
» Create valuable by products