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Improving faecal sludge dewatering efficiency of unplanted drying bed
By
Richard Amankwah Kuffour (MSc.)
A Thesis submitted to the Department of Civil Engineering, Kwame Nkrumah
University of Science and Technology
(KNUST)
in partial fulfilment of the requirements for the degree
of
DOCTOR OF PHILOSOPHY
Faculty of Civil and Geomatic Engineering
College of Engineering
March, 2010
ii
CERTIFICATION
I, Richard Amankwah Kuffour hereby declare that this submission is my own work
towards the PhD and that, to the best of my knowledge, it contains no material
previously published by another person nor material which has been accepted for the
award of any other degree of the university, except where due acknowledgement has
been made in the text,
Richard Amankwah Kuffour ----------------------- -------------------------
(20034866) Signature Date
Certified by:
Prof. Mrs. Esi Awuah -------------------------- -----------------------
(Principal Supervisor) Signature Date
Dr F. O. K. Anyemedu -------------------------- -----------------------
(Second Supervisor) Signature Date
Certified by:
Prof. M. Salifu -------------------------- -----------------------
Head of Department Signature Date
iii
DEDICATION
I dedicate this work to the Lord Almighty God.
iv
ACKNOWLEDGEMENTS
To God be the glory for the opportunity and strength given me to successfully go
through this research.
My sincerest gratitude goes to my supervisors Professor Mrs. Esi Awuah and Dr. F. O.
K. Anyemedu, of the Civil Engineering Department of KNUST who encouraged me
to undertake this project and whole-heartedly offered constructive suggestions and
criticisms and directed the research patterns of the project.
To Martin Strauss (formerly of SANDEC), Kone Doulaye, Agnes, Caterina and all
SANDEC team of EAWAG in Switzerland, I say a big thank you. But for your
guidance encouragement and sponsorship, this research would not have been
successful.
To Dr. O. O. Cofie, Benard Keraita, Amoah Philip, all of IWMI, not forgetting
Kwame, Maxwell, Lesley and all IWMI staff, I thank you for offering me free office
with computer and internet, library together with your advice and guidance.
To all my friends, Noah Adamptey, Daniel Sarpong, Oworae Alex, Sharon Quarshie
and others, God richly bless you for your countless contributions, encouragements and
assistances. To my colleagues at College of Agriculture, Asante – Mampong campus,
University of Education, Dr. Harrison Dapaah, Vincent, Eben, just to mention a few,
for your explanations, editing, data analyses, encouragement, prayers and support.
v
Mr. Bruce, Mr. Antwi, Mr. Botchwey and Kingsford all technicians of the Civil
Engineering Environmental Laboratory for their immense assistances, not forgetting
Mr. Gilbert Fiadzo of soils laboratory, for your explanations and assistance in the
analyses of the sand.
To my brothers, sisters, nephews and nieces, I extend my sincere thanks for your
prayers, assistances and contributions in diverse ways. Finally, I wish to express my
heartfelt gratitude to my wife, Joyce, my children, Isaac, Festus, Nancy and Blessing,
for their cooperation, patience, support and prayers.
vi
ABSTRACT
This thesis examines how to improve on faecal sludge dewatering efficiency of
unplanted filter beds to produce biosolids and less concentrated filtrate. The
experiment was conducted on bench scale drying beds constructed at the Kwame
Nkrumah University of Science and Technology campus. Local sand was graded into
particle size ranges of 0.1- 0.5 mm, 0.5 - 1.0 mm and 1.0 - 1.7 mm, with uniformity
coefficients of 2.422, 1.727 and 2.029, respectively. They were represented as filter
media, FM1, FM2 and FM3 respectively. Faecal sludge, consisting of public toilet
sludge and septage collected from cesspit emptiers discharging at Dompoase treatment
ponds in Kumasi, Ghana, were mixed in the ratio of 1:1 by volume, and was
dewatered using the three different filter media, FM1, FM2 and FM3 to determine
which one was most efficient. The Solid Loading Rate (SLR) of the faecal sludge was
varied in the phase two whereby public toilet sludge and septage, mixed in the ratio
of 1:1, 1:2 and 1:3 by volume representing SLR1, SLR2 and SLR3 respectively. These
were dewatered on filter medium one (FM1) which was selected in phase one. Six
cycles of dewatering were run for each of the phases. Percolate volume was measured
every 24 hours. The total solids (TS) of the faecal sludge used for dewatering varied in
every cycle so the TS was kept constant at 36.64 g/l as SLR1 and 26.93 g/l as SLR3
in all the cycles in the phase three to determine the effect of constant TS on the
dewatering process. Further improvement of the dewatering was investigated by
mixing sawdust with faecal sludge in phase four. Different percentages of sawdust,
50%, 100%, 150% and 0% (control) by weight of the TS of the faecal sludge, with TS
of 26.93 g/l which was selected in phase two, were mixed with the faecal sludge to
determine the effect of different quantities of sawdust as physical conditioner on the
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dewatering of faecal sludge. The dried biosolids obtained from the different phases of
dewatering were analysed for plant nutrients and heavy metals to determine their
agricultural potential. The dewatering on different filter media, FM1, FM2, and FM3
showed average dewatering times of 9.8, 9.9 and 9.1 days respectively without
significant differences (p=0.212). However the percolate quality showed significant
differences between the different filter media in the removal of TS, TVS, SS, COD,
DCOD and NH3-N with FM1 having the highest removal efficiency for each
parameter. Accumulation of organic matter in the top 10 cm of the filter bed indicated
that FM1 was least likely to clog since it had the least quantity of organic matter in the
sand. It also produced the largest quantity of organic matter and thus had the potential
to generate the most biosolids. The faecal sludge of SLR1, SLR2 and SLR3 dewatered
significantly at different average dewatering times of 7.2, 4.8 and 3.8 days
respectively. Removal efficiencies at the different solid loading rates, though very
high for TS, SS, TVS, COD, DCOD, NH3-N, did not show any significant difference.
Organic matter build up in the top 10 cm of the filter bed was least in SLR3, hence
least likely to clog the filter bed. Again, SLR3, SLR2 and SLR1 showed the potential
for annual generation of biosolids at 438, 421 and 379 (kg/m 2 /year) respectively.
Therefore SLR3 of faecal sludge was recommended for dewatering on the selected
filter bed.
When TS of the faecal sludge for dewatering was kept constant and the number of
cycles was increased to eight, FM1, FM2 and FM3, dewatering FS of SLR1 at
constant TS of 36.64 g/l improved their dewatering time to 8.9, 8.8 and 8.7 days
respectively while SLR3 with constant TS of 26.93 g/l, dewatering on FM1 had the
shortest dewatering time of 4.4 days. SLR3 was significantly most efficient in
removing TS, SS, TVS, COD and EC. Organic matter accumulation rate in the top
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10cm of filter bed was least for SLR3 followed by FM1, FM2 and FM3. The
percentage organic matter of the biosolid were 69, 68, 62 and 59, leading to
estimation of annual organic matter production of 334, 193, 202 and 177 kg
TVS/m 2 /year for SLR3, FM1, FM2 and FM3 respectively.
The sawdust-faecal sludge mixture of 50%, 100%, 150% and 0% TS of faecal sludge
dewatered at 5.3, 4.9, 3.9 and 5.6 days respectively with 150% being fastest to
dewater. The 150% sawdust-faecal sludge treatment was most efficient with respect to
removal of contaminant loads like TVS, SS, COD and NH3-N, but was least in TS and
EC removal. The 150% sawdust-faecal sludge mixture showed the least organic
matter accumulation rate in the top 10cm of the filter media, followed by the 100%,
50% and the 0% treatments. The percentage TVS of the biosolids produced were 70.1,
77.3, 80.6 and 66.3 for 50%, 100%, 150% and 0% sawdust-faecal sludge mixtures,
leading to annual organic matter estimation of 359, 567, 987 and 225 (kg
TVS/m 2 /year) respectively.
The agricultural potential of the biosolids analysed showed that, dried biosolids from
the filter beds had percentage carbon (C) ranging between 28% and 43.5% while
percentage nitrogen (N) in the same samples ranged between 1.82% and 3.53%
leading to C/N ratio, ranging between 8.7 and 23.9. The percentage phosphorus (P) in
the same samples ranged between 1.73% and 3.69% while the percentage potassium
(K) values were within the range of 0.66% and 1.67%. The maximum concentration of