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EFFECT OF ACID AND ULTRASONICATION PRE-TREATMENTS
ON THE LIPID EXTRACTION FROM PETROCHEMICAL INDUSTRY AND
MUNICIPAL WASTEWATER SLUDGES
Dilek AlperElif BabayiğitProf. Dr. Ayşen Erdinçler
Boğaziçi UniversityInstitute of Environmental Sciencesİstanbul, Turkey
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Outline
Aim of the study
Methodology
Materials and methods
Results and conclusions
Introduction
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Energy Scenario in the World
Currently 81% of all energy consumed worldwide is from fossil fuel sources. Renewable energy sources are expected to be 16.1% of world energy consumption in 2040.
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Energy Scenario in the World
Fossil fuel reserves are rapidly declining, especially oil and natural gas reserves approach critical levels.
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The fossil fuel sources will be
depleted in near future.
Increasing need for renewable energy sources
Energy from BIOMASS
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What is Biodiesel?
Biodiesel is an alternative fuel that may bederived from a variety of feedstock.
Lipid extraction is the first step of biodieselproduction.
Commonly produced by transesterification of pre-extracted oils with an alcohol in thepresence of a catalyst to generate the fattyacid methyl esters (FAMEs)
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Lipid Feedstocks
Edible plant oils• rapeseed oil
• sunflower oil
• palm oil
• soybean oil
• coconut oil
high cost of pure vegetable or seed oils, 70-85% of the overall biodiesel production cost
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Lipid Feedstocks
Non-edible plant oils• jatropha
• castor
• neem
• karanja
excessive cultivation
deforestation and destruction of the
ecosystem
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Lipid Feedstocks
Animal fats
Waste cooking oil
Microalgae
low quality the biodiesel consistency
high cost related with biomass production
Wastewater Sludge
in Turkey
Sludge production ≈ 299 ktons in 2017
Expected to 911 ktons in 2040
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Sludge as a Lipid Feedstock
Wastewater sludge is readily available in large quantities
Wastewater sludge is cheap or practically costless feedstockgenerated in WWTPs, therefore the cost of biomass production and land requirement is eliminated.
Wastewater sludge is non-edible lipid feedstock, therefore the competition with the food market is eliminated.
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Sludge as a Lipid Feedstock
Municipal (Domestic) lipids up to 30 %wastewater sludge (by wt)
Petrochemical WWTP lipids up to 40-60 % sludge (by wt)
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Aim of thisStudy
to explore lipid extraction from municipal and petrochemical industry WWTP sludges by using the novel direct liquid-liquid extraction method, which does not require expensive sludge dewatering/drying steps;
to investigate the effect of acid and ultrasonicpre-treatments on the lipid yields
to compare direct liquid-liquid lipid extractionmethod to standard reference drying method
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Materials and Methods
Sludge Samples:
•Municipal (Domestic) Wastewater Sludge •Primary Sludge : from the bottom of the primary clarifier in a biological wastewater treatment plant in İstanbul
•Petrochemical Industry WWTP Sludge: from the sludge thickening unit of the wastewater treatment plant of a petrochemical industry in Turkey
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Primary Sludge
• is a combination of floating grease and solids
• contains high lipid content originated from the adsorptionof lipids, in the form of: triglycerides, diglycerides, monoglycerides, phospholipids, free fatty acids (FFAs)
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Petrochemical Industry WWTP Sludge
• contains sludges from oil separators, primaryclarifier, and the waste activated sludge fromsecondary clarifier
• comprises of various organic and inorganiccompounds consisting: water-soluble metals,salts, phospholipids, suspended solids,petroleum hydrocarbons (PHCs), neutral lipidsand FFAs sourced from the waste activatedsludge oils that cannot be removed in WWTP.
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Sludge Characteristics
Parameter UnitPrimary sewage
sludge
Petrochemical industry WWTP
sludge
TS % 4.2 3.4
VS % 2.4 2.1
COD mg/L 40280 63220
sCOD mg/L 3090 10800
Viscosity mPa.s 8.0 52.8
pH - 6.2 6.8
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Pre-treatments
Acid Pre-treatment
• 0.1N HCl application to reach pH:2
Ultrasonication Pre-treatment
• 20 kHzfrequency• 200 W power output• 70% amplitude• 13 min• 15000 kJ/kg TS
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Lipid Extraction Methods
1. Direct liquid-liquid lipid extractionmethod
2. Standard drying method
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Standard Drying Method
Sludge samples
Acid pre-treatment
(HCl)
Drying with MgSO4.H2O
Solvent addition (hexane)
Soxhlet extraction LIPID
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Direct Liquid-Liquid Lipid Extraction Method
Sludge samples
Acid pre-treatment
Solvent addition (hexane)
Mixing at 200 rpm for 20 min
Settling at 60 rpm for 15 min
Filtering with 4µm filter paper
Application of anhydrous Na2SO4
Evaporating
LIPID
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RESULTS AND DISCUSSION
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Effect of Extraction and Pre-treatment Methods
Sludge typeExtraction method
Lipid Yield (%)(a)
Pre-treatment method
No-pretreatment
AcidUS (Ultrasonic)
Acid+US
Primary sewage sludge
Standard drying(b) 22.6 24.0 20.5 25.0
Direct liquid-liquid extraction
10.3 19.2 9.0 20.8
Petrochemical industry WWTP sludge
Standard drying(b) 21.4 23.7 29.1 33.1
Direct liquid-liquid extraction
30.5 34.8 30.9 45.2
(a) All transesterification experiments were performed at least twice.(b) Extraction according to standard MgSO4.H2O method, lipid yield on the basis of dry sludge.
+50%
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Comparison of Lipid Yields Primary Wastewater Sludge
0
5
10
15
20
25
30
Non-acidified Acidified Ultrasonication (US) Acid + US
Lipid yields, %
Standard drying method Direct liq-liq method
+102%+86%
-12%
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Comparison of Lipid Yields Petrochemical Industry WWTP Sludge
0
5
10
15
20
25
30
35
40
45
50
Non-acidified Acidified Ultrasonication (US) Acid + US
Lipid yields, %
Standard drying method Direct liq-liq method
+1%
+48%
+14%
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Efficiency of Extraction Methods
Direct Liquid-Liquid high lipid
Lipid Extraction Method low biological content
Feedstocks having;
Standard Drying Method high biological content
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CONCLUSIONS
Oily sludges from petrochemical industry WWTPs and sludges from primary settling tank of municipal WWTPs are lipid-rich feedstocks for biodiesel production.
Direct liquid-liquid lipid extraction method resulted with higher lipid yields for the petrochemical industry WWTP sludge having high lipid low biological content
Standard drying method is found to be more efficient forthe municipal sludge having high biological and relativelylow lipid content.
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CONCLUSIONS
Acid pre-treatment increased the lipid yields.
The ultrasonication pretreatment alone did not improve the lipid yields of municipal wastewater sludge samples.
The combined acidification/ultrasonication pretreatment caused to an important increase in the lipid yields of both sludge types.
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Taking into consideration economy of the process,liquid-liquid lipid extraction method may bepreferred as it eliminates dewatering/dryingsteps, contributing the 50% of the whole biodieselproduction cost.
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Prof. Dr. Ayşen Erdinçler
Bogazici UniversityInstitute of Environmental Sciences
Hisar Campus, TurkeyTel: +90 212 359 72 55Fax: +90 212 257 50 33
THANK YOU
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Biodiesel Production Yields
Sludge type Extractionmethod Yield (%)(a) Non-
acid. Acid US US+Acid
PrimaryWastewater
sludge
Standard drying(b)
Saponifiable 58.0 55.0 50.0 56.0
Biodiesel 13.1 13.2 10.2 14.0
Directliquid-liquid
extraction
Saponifiable 54.0 68.0 61.0 67.0
Biodiesel 5.6 13.1 5.5 14.0
PetrochemicalIndustry WWTP
sludge
Standard drying(b)
Saponifiable 65.0 66.0 67.0 68.0
Biodiesel 13.9 15.7 19.7 22.5
Directliquid-liquid
extraction
Saponifiable 68.0 71.0 69.0 69.0
Biodiesel 21.0 24.7 21.4 31.1(a) All transesterification experiments were performed at least twice.(b) Extraction according to standard MgSO4.H2O method, lipid yield on the basis of dry sludge.