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Unit of Functional BionanomaterialsSchool of Biosciences
Mark D. Redwood, Kevin Deplanche, Angela Murray, Iryna P. Mikheenko, Ping Yong, Neil J. Creamer, Rafael Orozco, Oluwakemi Lowal, Lynne E Macaskie.
19th May 2010
Prof Lynne E Macaskie
Applied Microbiolo
gy
Applied Microbiolo
gy
Bio-energy
Bio-remediation
Bio- nanocatalyst
Making bioenergyEscherichia coliRhodobacter sphaeroides ; capsulatusMaking bionano catalystDesulfovibrio desulfuricans ; fructosovoransEscherichia coliRalstonia, Rhodobacter spp, Micrococcus spp.,
Shewanella, Geobacter, Arthrobacter(Making ion exchangers)
DarkFermentation
Photo-Fermentation
Sugarywastes
H2
Organicacids
UK [food industry + domestic] = 24 M tpa
Potential to produce 280 M kg of bio-H2
Energy value: 5.6 TWh (terawatthour) and heat
13% of 2020 target◦ 15% renewable sources.
Total waste is ~110 M tpa inc. agricultural and sewage
Unique combination of advantages:◦ Renewable/sustainable energy sources
Organic matter and sunlight◦ Inherently free of fuel cell poisons
CO, H2S
◦ Waste disposal Food waste Agricultural residues
◦ Simple/cheap process Ambient temperature & pressure
Bench scale (1ml-20L) Pilot scale (120 L)
Ideally:1 Glucose 2 H2 + 1 acetate + 1 ethanol + 2 CO2
We select E. coli because◦ Fast aerobic growth◦ Tolerance to O2 during anaerobic fermentation
◦ Best tolerance to H2 partial pressure◦ No sporulation◦ Best-characterised genetic background for GM
E.g. removal of uptake hydrogenases◦ ‘electrotolerance’
AnionCation
Anion-selectivemembrane
Electrodialysis uses an anion selective membrane and direct current
Organic acids cross the membrane due to negative charge
FermentationConcentratedorganicacids
- +
+/-
WasteFruit
Manual chopping
1st Press
Juice
Pressings Wash
Water
Infusion
2nd press Washed Pressings
Hot Compressed Water (HCW)
Hydrolysate
Detoxification
Fermentation
Water
Stones Insolubles and by-
products
Solid residues
Organic acids H2 + CO2
Anoxygenic photosynthesis
Purple non-sulphur bacteria◦ Rhodobacter spp.
High yield, broad substrate range◦ e.g. Lactate 6 H2
H2 produced by Nitrogenase enzyme◦ Very sensitive to NH4
+
◦ Select wastes with high C/N
Light conversion efficiency◦ Up to ~5%
Logging equipment for light intensity and temperature.
250 ml 250 ml reactors + reactors + water-water-jacketjacket
March, June and October
Water heater pumps 30 °C water to the jackets
Tubular arraySimulates 0.5 m2 of sunlit
areaVolume : up to 50 LLamps deliver
programmed light patterns
Simulates any location or season
Equatorial
UK
Equatorial
UK
MethodNet energy / areakWh/day/hectare
Source
UoB’s bio hydrogen 670 (UK) (+ gate fees)Biowaste2energy
Photovoltaics (PV) 665 (Bavaria)Bavaria Solarpark
Wind 480 (UK, on shore) MacKay (2009)
Anaerobic Digestion (AD) 425 (+ gate fees)Vagron, Netherlands*
Crop-derived bio-fuels ~120 (UK) MacKay (2009)
Alga-derived bio-diesel Purportedly better than crops
* Including parasitic energy and total site area. Published values use the raw energy generated and only the space occupied by the digester.
When Biology meets Nanotechnology◦ Reduction of metal precursors using bacterial
enzymes yields highly active nanoparticles (NPs) at the cell surface
Bacterial cell
Bacteria concentrate precious metals
Hydrogenase enzymes
2H+ + Pd0(s)
Palladised cells of D. desulfuricans
Nanoparticles grow and erupt from the cells
Stabilised nano-Pd(0) crystals
bound to cells. Similar results with Pt(0)
Atom-scale resolution shows crystal structure; faces are
clearly visible (5 nm Pd-nanoparticle)
Biocatalyst manufacture process optimised for PGMs◦Pd, Pt, Au
Monometallic and bimetallic Manufacture can be coupled to biorecovery of
metals from wastes◦‘Green chemistry’◦Lower the threshold of economic recovery of
PGMs
Advantages over conventional chemical catalysts◦Cheap(er), “green” manufacturing process◦Easy to scale up◦Excellent monodispersity of NPs◦Bacterial support doesn’t leach metals◦Can be recycled◦Exhibit different properties from chemical
catalysts◦Active in a broad range of reactions
Manufacture of platform chemicals◦ Selective hydrogenations (Pd, Pt)
E.g. Heck coupling (pharma)◦ Selective oxidations (Au, Au/Pd)
Perfume industry, food additives… ◦ Remediation of recalcitrant compounds (TCE)◦ Green energy
Conversion of biodiesel wastes (glycerol-Au) Automotive catalysts
Reduction of pollutant emissions (CO, NOx) Improvement of performances
Fuel cells electrocatalysts (PEMFC)
Tested catalyst by recycling in a series of reactions
Compared selectivity and conversion
With Pd/C, rate drops substantially with each run Key feature of BioPd: increased recyclability – shelf life
CO chemisorption experiments shows bio-Pd contains much smaller Pd particles than Pd/C
Bio-Pd Pd/C
Metal Dispersion (%) 67 3
Metallic Surface Area(m²/g sample)
15 0.6
Metallic Surface Area:(m²/g metal)
297 11
Active Particle Diameter (nm)
2 45
Why is there a difference in activity between bio-Pd and Pd/C? Smaller particles; greater proportion of corner atoms and adatoms
more active in Heck coupling (Augustine et al., J. Mol. Cat. A., 1995, 95, 277-285)
corner atom
adatom
bacterial cell Pd(II) Pd(0)
Soluble Pd(II) complexes are the catalytic species1. Solid Pd(0) Soluble Pd(II) complexes2. catalyses Heck coupling3. Pd(II) Pd(0) at the end of the cycle
bacterial cell
Pd(II) Pd(0)
Carbon Carbon
The Pd particles may redeposit on the support’s surface directly on top of other Pd particles already on the support
Pd particles reform on other Pd particles, thus the particle size grows
Zhao et al., J. Mol. Cat. A., 2002, 180, 211-219
BioPd maintains small particle size through 6 runs Initially smaller particles Redeposition onto biomass
Pd(II) Pd(0)
Carbon Carbon
Bimetallic catalyst with high numbers of Au core/Pd shell NPs
500 nm
HAADF analysisTEM analysis
Benzyl alcohol Benzyl aldehyde
Toluene
Benzene
Benzoic acid
Benzyl benzoate
Selective oxidation of benzyl alcohol to benzaldehyde
High constant selectivity towards benzylaldehyde
Work in progress on a range of alcohols
5% Pd/C
Area of Research
Recovery of Platinum Group Metals
from Secondary Sources
Physical Processing to
Upgrade Metals
Chemical Leaching to
Solubilise Metals
Recovery of Metals using
Bacteria
Added Value End Product
Incinerator Ash Road Dust Industrial Slag Materials Electronics scrap
Electrostatic SeparationElectrostatic separations separate one material from another by exploiting the difference in electrical conductivity.
High Tension roll separator was tested using a titanium roll set at 53rpm
Feed Hopper
Ionising electrode
Static electrode
Brush
Earthed titanium roll
Vibratory feeder
Insulators ConductorsMiddling
Microwave Leaching of PGM sources
Road Dust
In the UK Local Authorities collect road dust They store it at regional depots It is then sent for expensive landfill
Road Dust in UK
•Valueless Material
•Disposal costs associated with it
•Research has shown PGM levels in road dust of 1.8 parts per million (ppm)
•Primary PGMs mined in South Africa at 4-10 ppm from deep underground
•PGMs also mined in Canada at less than 1ppm
•Therefore Road Dust levels comparable to primary low grade ores
PGMs in Road Dust
2 spin out companies
◦ Biowaste2energy Ltd◦ Bioenergy from organic wastes
◦ Roads2Riches Ltd◦ Precious metal recovery from wastes
www.bw2e.com
Electrical Load
Anode
Cathode
Proton exchange membrane
H2
2 H2 → 4 H+ + 4 e-
O2 + 4 e- + 4 H+ → 2 H2O
H+
O2
Pt catalyst
e- flow
Pt catalyst
2 Requirements: PGM nano-catalyst and clean hydrogen
Aim: Bio-based fuel cell using biohydrogen and bio-recovered Pt
Fuel cell catalyst Power output (Pmax, mW)
H2
Bacteria
Organicwaste
Pre-treatment
Bioenergyreactors
CleanEnergyPEM-FC
Metalwaste
CatalystMetallised cells
Sorption &reduction
Chemicalindustry
43
1. Grow Serratia biofilm (3L bubble column reactor)2. Supply biofilm with G2P and Uranium3. Phosphatase forms Hydrogen Uranyl Phosphate (HUP)
(Alternatively Zirconium phosphate)
4. Result: “Primed” biofilm, ready to adsorb radioactive metals – e.g. Strontium, Cobalt, Caesium
Sodium glycerol 2-phosphate (G2P)
Periplasmic phosphatase
Phosphatase within extracellular polymeric substance
HPO42-
Bacterial cell
UO22+
HUO2PO4.nH2O (HUP)
2 cm
Reactor volume: ~8 mL
5 cm
Polyurethane foam coated with primed biofilm
Cleaned outflow solution
Contaminated
inflow solution
Examples of inflow radioactive metals:60Co, 85Sr and 137Cs
15ml column volume
Tests performed at the Korea Atomic Energy Research Institute (KAERI).
Removal of 60Co, 85Sr and 137Cs from simulated radioactive waste solution by ion exchange using reactors containing HUP supported on biofilm
Simulated radioactive waste: 137Cs, 85Sr and 60Co (0.333 mM), pH 5.44, flow rate 10 mL/hBreakthrough capacity: 137Cs = 0.11 mmol, 85Sr = 0.055 mmol, 60Co = 0.055 mmol Efficiency: 97%
3 integrated processes3 inter-related themes
Organicwaste
Pre-treatment
Sugarfeed
Bio-process
H2
EnergyPEM-FCMetalwaste
Bacterialcells
CatalystPd/Pt coated cells
Uranylnitrate
Sorption &reduction
Ion exchangerHUP-coated cells
Sorption & reduction
Decontamination of nuclear waste
Mol of
H2 e
quiv
ale
nt 1.5
1
0.5
2