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July

2020

HYDROCARBON

ENGINEERING

46

dewatering sludge to expose new sections of the belt for free

water to drain through. In addition to exposing sections of the

belt, the shifting action caused by the plows also turns the

sludge, creating a path for the free water that pooled on top

of the sludge to bypass flowing through the solids and drain

much more quickly. Modifications to the plows generally

consist of adding additional rows of plows and aligning the

plows to get maximum shifting of the solids.

Results obtained through GDS

optimisation

In two separate industrial wastewater treatment sites, the GDS

of the BFPs on site were optimised. System 1 adjusted the

distribution pipe to distribute evenly across the entirety of the

belt, as was mentioned previously, but also installed an

additional row of plows to accompany the four rows already

present. System 2 had a distribution system that evenly

distributed the solids across the entirety of

the belt, but lacked plows to assist the

drainage of free water. In this system,

temporary rows of plows were installed on

the press. In both instances, no other

changes were made to the BFP operation

and both systems experienced a 1 – 2%

increase in cake solids as soon as the

changes were made.

System 1 saw an increase in cake solids

percentage from 15.97% to 17.3%. This

resulted in a 7.7% decrease in the overall

amount of cake shipped off site for disposal

and a 9.1% decrease in lb of water shipped

off site for disposal with the sludge

(Figure 2).

At the average cost to dispose of solids

being US$40.92

5

in the region this site is

located, the optimisation of the distribution

section cut the price for disposing of 1 t of

biological solids out of the biological

treatment area and into landfill by US$19.64.

System 2 saw an increase in cake solids

percentage from 12.68% to 14.49%. This

resulted in a 12.5% decrease on the overall

amount of cake shipped off site for disposal

and a 14.3% decrease in lbs of water shipped

off site for disposal with the sludge

(Figure 3).

At the average cost to dispose of solids

being US$40.92 in the region this site is

located, the installation of the plows into

the GDS cut the price for disposing 1 t of

biological solids out of the biological

treatment area and into landfill by US$40.51.

Conclusion

Rising costs of solids disposal across the US

demand greater performance and efficiency

from the solids dewatering units in

wastewater treatment plants in order to

control costs. Inexpensive improvements

and mechanical optimisations to the GDS

result in tens of thousands of dollars in savings by improving

the overall performance of BFPs, with little to no costs after

the installation and implementation of the upgrades. These

improvements pay for themselves in a matter of months and

continue to provide benefits for years after installation.

References

1.

‘Solids Process Design and Management’, Water Environment

Federation, (2012).

2.

ANDREOLI, C. V., SPERLING, M. V., and FERNANDES, F., ‘Biological

Wastewater Treatment Series: Volume 6 Sludge Treatment and

Disposal’, (2007).

3.

TUROVSKIY, I. S. and MATHAI, P. K., ‘Wastewater Sludge Processing’,

(2006).

4.

‘Report on the management of wastewater treatment sludge

and septage in Vermont: an analysis of the current status and

alternatives tio land application’, Conservation, Agency of Natural

Resources Department of Environmental, (2015).

5.

KANTNER, D. L. and STALEY, B. F., ‘Environmental Research and

Education Foundation (2019) “Analysis of MSW Landfill Tipping Fees

- April 2019”’, (2019).

Figure 3.

Results for System 2.

Figure 2.

Results for System 1.