Downstream processing for Polyhydroxyalkanoates from mixed - - PowerPoint PPT Presentation

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Downstream processing for Polyhydroxyalkanoates from mixed - - PowerPoint PPT Presentation

Session XXIV Recovery of materials from wastewater & sludge Sludge management Downstream processing for Polyhydroxyalkanoates from mixed microbial cultures: Study of microbial activity inhibition, polymer recovery and characterizations


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Downstream processing for Polyhydroxyalkanoates from mixed microbial cultures: Study of microbial activity inhibition, polymer recovery and characterizations

1Department of Chemistry University of Rome La Sapienza

laura.lorini@uniroma1.it

Session XXIV Recovery of materials from wastewater & sludge – Sludge management

  • 1L. Lorini, 1F

. Valentino, 1G. Bifolchi, 1A. Martinelli, 1M. Majone

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Polyhydroxyalkanoates (PHA)

  • Biodegradable

commodity film

  • Packaging interlayer film
  • Specialty durables (such

as electronics)

  • Slow C-release system

for groundwater remediation

(Kunansudari, Exp Polym Let 2010)

Heraklion2019 28th June 2

Product related Pro’s Family of copolymers with tunable composition Main constituent of several bioplastics

non biodegradabl e, mechanical recycling biodegradab le, recycling with organic waste Bio-based feedstock Biodegradabilit y Biopolym ers starch blends, PLA, PHA Bio-PE (PP/PVS), biobased PET PE, PP, PS, PVC, PET ecc. PBAT, PBS, PCL Oil-based plastics Bio-based feedstock and biodegradability

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PHA production from MMC and organic waste

Stage III: PHA production Stage II (SBR): biomass selection/ enrichment (ADF) Acidogenic Fermentation Sludge from wastewater treatment plant VFA VFA MMC Activated sludge PHA-rich biomass Solid fraction Liquid fraction Anaerobic Digestion Energy Nutrients PHA extraction

Biodegradab le bioplastics

PHA processing Organic fraction of municipal solid waste (OFMSW)

Heraklion2019 28th June 3

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Pilot platform

Wastewater Treatment Plant in Treviso (North-East

  • f Italy)
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Aim of the study

Optimization of a stabilization method

 Infmuence of pH ➔ H2SO4; NaOH  Oxidation➔ NaClO  Excess of substrates  Thermal treatments➔ oven dried at 70°C (with or

without shock at 170°C) Innovative extraction and recovery methods

 Non-chlorinated solvent: ethyl acetate

Characterization of extracted polymer:

 GC-FID ➔ purity, recovery yield and monomeric

composition

 Capillary viscosimetry ➔ molecular weight  DSC ➔ thermal properties

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Selection of PHA-producing biomass (SBR)

Operative cycle (12 h)

Feeding= 10 min Reaction 1= 140 min Withdrawal= 3 min Nitrogen feeding= 5 min Reaction 2= 562 min

V = 1L Organic load rate (OLR) 4.25 gCOD/L d VFA (85% Acetic acid; 15% Propionic acid) T= 25°C

Heraklion2019 28th June 6

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PHA accumulation step

  • Batch reactor V= 0.5L
  • 6h test
  • Multispike strategy (85% Acetic acid;

15% Propionic acid)

Selection (SBR) PHA storing biomass Accumulati

  • n

(Batch) PHA-rich biomass

1 2 3 4 5 6 7 500 1000 1500 2000 2500

PHA content

t (h) PHA mgCOD/L

VF A

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Stabilization tests

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0% 10% 20% 30% 40% 50% 60% 70% 80% 90% 100%

End of batch test Centrifuged 170°C+70°C 70°C

P H A t / P H A e n d o f a c c u m u l a t i o n

0,5 1 1,5 2 2,5 3

0% 2000% 4000% 6000% 8000% 10000% 12000%

time (h)

PHA t /PHAend of accumulation Two kinds of thermal treatment

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Extraction and characterization

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Purity (PHA %w/w) 95.3 % (CHCl3); 85.2 % (NaClO) Recovery yield (%w/w) 83.2 % (CHCl3); 87.4 % (NaClO) 5 different batches (Pilot scale Batches 11, 15, 19, 22, 24) and 1 batch (Lab scale) thermally stabilized Soxhlet extraction with CHCl3 Oxidation with NaClO

  • B. 11
  • B. 15
  • B. 19
  • B. 22
  • B. 24 Lab scale

50000 100000 150000 200000 CHCl3 NaClO Mv (KDa)

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Batch 11 thermally stabilized Extraction in a pressurized steel reactor with Ethyl acetate (100 and 125°C) for 1h Residues extracted with CHCl3

Non-chlorinated solvent extraction

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Conclusions and future prospectives

  • Thermal treatment applicable at pilot scale
  • NaClO gave results comparable to traditional chloroform

extraction

  • Ethyl acetate selectively extracts shorter chains
  • Evaluation of the efgects of thermal treatment on the

polymer, in comparison with an acidifjcation method applied at pilot scale

  • Optimization of Ethyl acetate extraction and use of other

non-chlorinated solvents

Heraklion2019 28th June 11

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Thanks for your attention