Date post: | 10-Jan-2017 |
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‘Sustainable Approach Of Recycling Palm Oil Mill Effluent Using Integrated Biofilm - Membrane
Filtration System For Internal Plant Usage’
Student Sajjad Khudhur AbbasSupervisor Dr. Teow Yeit HaanCo-supervisor Prof. Abdul Wahab bin Mohammad
Research Title‘Final
Presentation’
By
In Malaysia, oil palm is a very significant crop. In the worldwide, the biggest palm oil exporter and producer is Indonesia and Malaysia is the 2nd exporter and producer. The production of crude palm oil (CPO) was increased significantly from 92,000 tonnes in year 1960 to 17.6 million tonnes in year 2009, The process to extract the palm oil needs massive and huge water quantity to sterilize the fresh fruit bunches (FFB) and clarify the extracted oil.
Palm Oil in Malaysia SAJJAD K. A.
3rd Presentation
POME treatment
Palm Oil Mill Effluent (POME)
95-96% of water
0.6-0.7% of oil
2-4% of suspended solids
POME highest sources
Clarifier sludge
hydro cyclone
sterilizer condensation
SAJJAD K. A. 3rd
PresentationPOME
treatment
Environmental impact
)Ma A. N., 2000 (
)Singh G. a., 1999 (
The stocks of local fish in lakes and rivers are declining
Bathing and water sources turned into
brown colour smelt foul
Fresh POME
Acidic Colloidal Suspension
Hot
Brownish
High Solids Amount (40,000 mg/l)
COD (50,000 mg/l)
BOD (25,000 mg/l) ref
SAJJAD K. A. 3rd
PresentationPOME
treatment
Problem Statement
Briefly, the highly polluted wastewater is causing a severe pollution to the :
Waterways
Aquatic Habitats Impacted Human Health
Affected Aquatic Life
SAJJAD K. A. 3rd
PresentationPOME
treatment
Zero waste energy
POME Treatment system
Treated Water
Biogas
POME
SAJJAD K. A. 3rd
PresentationPOME
treatment
Sludge
Myth or Fact?
Available POME treatment techniques
Anaerobic contact process
Continuous stirred tank reactor (CSTR)
Up-flow anaerobic sludge fixed film (UASFF)
Up flow anaerobic sludge blanked (UASB)
Fluidized bed
Anaerobic filtration
Conventional anaerobic digestion (Digester and pond)
Conventional anaerobic digestion (Digester and pond)
Aerobic
Evaporation
Anaerobic
Membrane
Biofilm
Biofilm bacteria (Biological Treatment) integrated with Membrane Technology is based on WHAT FACTORS ? ANS:• COST EFFECTIVE• REQUIREMENTS• FLEXIBILITY • SIMPLICITY • CLOSED OR OPEN
SYSTEM N0TE: UPON our knowledge and research, There is no previous work had or have done on using integrated biofilm-Membrane.
SAJJAD K. A. 3rd
PresentationPOME
treatment
Biofilm technique integrated with Membrane
Membrane techniqueBiofilm technique
SAJJAD K. A. 3rd
PresentationPOME
treatment
Biofilm technique integrated with Membrane
Membrane techniqueBiofilm technique
Swimming
Attachment EPS
Feeding
Decomposition
Treatment Process
Kind – Cross flow Filter – Nano filter (NF)
Feed
Out
let
SAJJAD K. A. 3rd
PresentationPOME
treatment
Process Tension Factors
Membrane foulingBiofilm Bacteria dead lack
SAJJAD K. A. 3rd
PresentationPOME
treatment
PROCESS SETTING
Biofilm technique Membrane technique
Parameter Value Acclimatization duration
Unknown
Treating period Unknown Black media amount
328 pieces
White media amount
126 pieces
Raw POME volume 2 litres Raw POME COD 6630 mg/lTemperature Ambient
Parameter Value Pump pressure 3 barTemperature 24.1 CInlet POME COD 923 mg/lFilter Nano
SAJJAD K. A. 3rd
PresentationPOME
treatment
TREATMENT SCHEMESAJJAD K. A.
3rd Presentation
POME treatment
Be confident By measuring Parameters !
DO
CODTSS MLSS
NH3-N
PH
SAJJAD K. A. 3rd
PresentationPOME
treatment
Results SlideSAJJAD K. A.
3rd Presentation
POME treatment Acclimatization Stage ‘Hexafilter media’
Test\Day
1 3 5 7 9 11 13 15 17 19 21 23 25 27
COD 6630
3680 3440 3101 2908 2421 2220 2201 2400 2410 2409 2430 2190.3
2215
MLSS *103
12.10
15.10
9.80 6.50 3.90 3.30 3.00 2.70 3.23 3.66 3.07 2.45 3.26 3.12
NH3-N
970
350 309 287 240 227 226 200 193 121 112 109 90 81
Turb. 3740
1108 655 325 190 133 113 110 108 152 119 110 79 66
1
Acclimatization Stage ‘Black media’Test\Day
1 3 5 7 9 11 13 15 17 19 21 23 25 27
COD 6630
3550
3340 3010 2905 2901 2900 2769 2630 2510 2484 2450 3010 3005
MLSS *103
12.10
13.10
10.50
8.77 6.10 5.90 5.46 4.23 3.20 3.23 3.01 2.96 2.20 2.00
NH3-N 970 330 295 260 233 218 210 177 153 89 95 102 75 63Turb. 374
0998 845 755 598 357 293 175 113 130 89 60 20 15All in mg/l, except Turbidity
in NTU.
Results SlideSAJJAD K. A.
3rd Presentation
POME treatment
Biological Treatment Membrane
RawPOME
Hexafilter Black media NF UnitsTest 24 hr 48 hr 72 hr 24 hr 48 hr 72 hr -COD 1450 760 1130 850 690 910 1040 19 mg/lMLSS 0.006 0.0031 0.0025 0.0025 0.0035 0.0026 0.0032 0.0003 mg/lNH3-N 101 93 100 107 102 86 93 1.19 mg/l
pH 8.021 7.258 7.422 7.651 7.654 7.973 7.855 6.473 -TSS 290 140 420 405 340 470 410 0 mg/lDO 2.03 1.88 2.49 2.71 2.38 1.79 2.57 4.44 mg/l
Turbidity 87.9 140 122 93 130 111 76 0.381 NTU
2
HexafilterBlack media Membrane
Black Media
Biofilm carriers at the 2nd day of the bacteria growth
stage
Bacteria growth after 15 days at the media surface
Bacteria growth after one month at the media surface
Footages from different sections
Footage (Black Media) SAJJAD K. A. 3rd
PresentationPOME
treatment
Hexafilter Media
Biofilm carriers at the 2nd day of the
bacteria growth stage
Bacteria growth after 15 days at the media surface
Bacteria growth after one month at the media surface
Footages from different sections
Footage (Black Media) SAJJAD K. A. 3rd
PresentationPOME
treatment
Footages (Treated POME samples ) RAW POME
Distilled
POME
H media
B media
Membrane
SampleThe sample is following which standards?
Standards
RAW POME
Diluted POME
H media
B media
Membrane Sample
12 Slightly3 Slightly4 Slightly56 Slightly Slightly789
1011 Slightly SlightlyNo Definition 1 NWQSFM CLASS I2 NWQSFM CLASS IIA3 NWQSFM CLASS IIB4 NWQSFM CLASS III5 NWQSFM CLASS IV6 NWQSFM CLASS V
No Definition 7 DOE CLASS I8 DOE CLASS II9 DOE CLASS III 10 DOE CLASS IV 11 DOE CLASS V
SAJJAD K. A. 3rd
PresentationPOME
treatment
Result’s Closer LOOK
Biofilm bacteria treatment is complicated
since the treatment is wobbling
Membrane is so easy to be blocked
This integrated system won’t give product with
certain properties
This integrated system needs Control system
Its possible and better to use low level membrane like macro but the treated wastewater won’t be same
quality as the Nano.
SAJJAD K. A. 3rd
PresentationPOME
treatment
CONCLUSION
surface area
crimpy surface
narrow corners
Mixing
Moisture
NF membrane
SAJJAD K. A. 3rd
PresentationPOME
treatment
Future studies, endorsing and recommendations
SAJJAD K. A. 3rd
PresentationPOME
treatment
Series reactors
Sedimentation system
Catalyst
Fixed temperature
Deep reactor for biofilm growth stage
Short depth reactor for POME treatment stage
Closed system
Treatment age not longer than 24 hours
Using media with high surface area Endorsements
The Decree
From Standards side As a Scientist !
Strongly Definitely
SAJJAD K. A. 3rd
PresentationPOME
treatment
Global WarmingSAJJAD K. A.
3rd Presentation
POME treatment
Temperature rising
rising sea level
Floods
Heat waves
Extinctions of animals and plants
Desertification
Q & A
SAJJAD K. A. 3rd
PresentationPOME
treatment
THANK YOU
SAJJAD K. A. 3rd
PresentationPOME
treatment