Anaerobic Digestion of Lipids - WordPress.com · Anaerobic Digestion of Lipids:! the development of...

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Anaerobic Digestion of Lipids: the development of a multifaceted solution B. Conall Holohan

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Page 1: Anaerobic Digestion of Lipids - WordPress.com · Anaerobic Digestion of Lipids:! the development of a multifaceted solution! n! Focusing on AD solution to dairy wastewater lipids

Anaerobic Digestion of Lipids:!the development of a multifaceted solution!

B. Conall Holohan!

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Focusing on AD solution to dairy wastewater lipids

- !Microbial Communities

and !Reactors!

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Wastewater Treatment!Anaerobic Digestion!

!

-  Energy neutral/positive!-  No by-products (sludge)!-  Small land area needed!-  Enclosed (no-odours)!

Efficient !Can become an income provider.!

Activated Sludge !!!

•  Energy expensive!•  Large volume of sludge produced !•  Large space needed!•  Odour producing!!

Inefficient!Current practice!

Figure: Cheung et al. (2013)!

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Dairy Industry!

•  Ending of the EU quotas!o  Predictions 2020: 50% increase in production.!

•  High level complex wastewater produced.!

•  Outdated WW treatment systems.!

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Lipids in Dairy WW!•  Lipids are removed - dissolved air flotation (DAF)!

•  Causes foaming in activated sludge treatment!

•  ‘Treatment’: Removed & landspread with the sludge from aerobic treatment.!

•  Wasted resource: Energy possibility is high!

Figure: Bioscience Inc. (2012)!

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Biogas Potential from Lipids!

Carbohydrate!

Lipid!

Protein!

Biogas (l/g)! Methane (%)!

0.830!

69.5!1.125!

50.0!

68.8!0.921!

Amended from Alves et al. (2009).

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AD of Lipids!Challenging!

•  Inhibition & Accumulation!•  Floatation of granules!•  Difficulty in degradation!

•  Current practice:!•  Non-treatment/separation!•  Long treatment time (weeks)!

Lipids!

LCFAs!

VFAs!

Methane!

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Aim of Reactor Trial: !Identify the optimum anaerobic

reactor design.!& investigate the effect(s) of Trace Element addition!

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3 Reactors !R1 - UASB! R2 - UASB-Filter! R3 - EGSB!

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Trial Conditions!

•  Wastewater: “Raw” - Post-screening/Pre-DAF Treatment!

•  Sludge: Granular - Carbery Co. Cork!

•  Began @ 72hr HRT & 1.4 OLR!

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% C

OD

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oval!

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UASB!UASB-Anaerobic Filter!EGSB!

>70% Total COD Removal!

Trac

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t Add

ition

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>70% Soluble COD Removal!

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Poor Lipid Removal!

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R1!UASB!UASB-Anaerobic Filter!

Addition of TE = Lipid Removal!

TE Addition!

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Biogas Production!Pre TE Addition!

•  Consistent > 60 % Methane concentration!

•  Biogas conversion efficiency: ~50%!

Post TE Addition!

•  Consistently >60% Methane concentration!

•  Volume of biogas increased significantly!

•  Biogas conversion efficiency: >70%!

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Trace Element Effect..!

•  Shown preliminarily by Karlsson et al (2012)!

•  Addition of Fe; Co; Ni increased the methane yield!

•  Oleic Acid: 59% +/- 5% Increase!

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Further TE tests!•  Degradation Tests!

•  Oleate (LCFA: C18)!•  Skimmed Milk Powder (SMP) !

•  Aims: !1.  Replicate results seen in reactor trial!2.  Compare various TE compleations: !o  Shelton & Tiedje (1984) !o  Banks et al. (2012)!

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0.0!

13.3!

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0! 2! 4! 6! 8! 10! 12! 14! 16! 18!Time (hours)!

Blank!ST!Banks!

Increase in SMP Degradation Rate with TEs!

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Increase in Oleate Degradation Rate with TEs!

0.0!

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45.0!

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Banks!ST!Blank!

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Ultra-Sonication (US)!

•  Increases surface area (2.3X)!

•  Cracks/Craters formed!

•  Permeability increases 37%!

Figure: Cho et al., Bioresource Technology, (2013).!

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Positive Effect of US!30.3% ! 9.4%!

35.4%! 2.3%!

Increases in biogas production when US applied.!

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Following 16 days!% Increase in CH4 production!

•  Glucose: 70.4 %!

•  SMP: 59.4 %!

•  Oleate: 53.6 % !

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Conclusions!

!!

Reactor Design can have an important positive effect.!!

T.E.s have a positive effect on the degradation of lipids. !!

Ultrasonication has a positive effect on the degradation of Oleate. !!!

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With thanks to… !

•  Supervisor: Prof. Vincent O’Flaherty!

•  Dr. Dermot Hughes !

•  Dr. Si-Kyung Cho!

•  Dr. Florence Abram!

Nicholas Hogan!&!

Stephen Moloney!