utilization of waste in industrial (white) biotechnology
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Utilization of Waste in Industrial (White) Biotechnology. White Biotechnology . is an emerging field within modern biotechnology that serves industry. - PowerPoint PPT PresentationTRANSCRIPT
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Utilization of Waste inUtilization of Waste inIndustrial (White) BiotechnologyIndustrial (White) Biotechnology
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White Biotechnology White Biotechnology 2
• is an emerging field within modern biotechnology that serves industry.
• It uses living cells like moulds, yeasts or bacteria, as well as enzymes to produce goods and services. Living cells can be used as they are or improved to work as "cell factories" to produce enzymes for industry.
• White Biotech can help realize substantial gains for both environment, consumers and industry.
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BiotechnologyBiotechnology
GreenGreenAgro-FoodAgro-Food
RedRedHealth CareHealth Care
WhiteIndustrial
HealthHealth Unmet NeedsUnmet Needs
EconomyEconomySustainabilitySustainabilityUsing nature’s toolset
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4Industrial (White) Biotechnology Industrial (White) Biotechnology
SugarsBiofuelsBiomaterialsBiochemicals
Cell factories
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5The IB Value ChainThe IB Value Chain
BiofuelsH2
Ethanol
SugarsFeedstocks-Renewable- Fossil
BiochemicalsFood IngredientsPharmaceuticalsFine Chemicals
BiomaterialsPolylactic acid
1,3 propane diolPHAs
Bioprocesses
Bulk
Fine
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Cleaner and more (cost) efficient ways of making:
Faded jeansDetergentsPlasticsVitaminsAntibioticsFuelBiosteelBiobatteriesDNA computers
Industrial BiotechnologyIndustrial BiotechnologyPr
e se
Pre s
entnt
Fut u
rFu
t ur
ee
Reduced Reduced environmental foot-environmental foot-print up to 20 – 60 %print up to 20 – 60 %
Added Value ofAdded Value of11-22 billion € per 11-22 billion € per
YearYear
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IB: three IB: three P’sP’s go hand in go hand in handhand
sustainability
Profit
People
Planet
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8The IB Value ChainThe IB Value Chain
BiofuelsH2
Ethanol
SugarsFeedstocks- Renewable- Fossil
BiochemicalsFood IngredientsPharmaceuticalsFine Chemicals
BiomaterialsPolylactic acid
1,3 propane diolPHAs
Bioprocesses
Bulk
Fine
Strong points Europe• Enzymes• Biochemicals
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9The IB Value ChainThe IB Value Chain
BiofuelsH2
Ethanol
SugarsFeedstocks-Renewable- Fossil
BiochemicalsFood IngredientsPharmaceuticalsFine Chemicals
BiomaterialsPolylactic acid
1,3 propane diolPHAs
Bioprocesses
Bulk
Fine
Biomass
Bioenergy
B & B
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10Developing a Strategic Research Agenda and Roadmap (1)Developing a Strategic Research Agenda and Roadmap (1)
Main R&D objectives
Strain, biocatalyst & process optimization
Novel and/or improved functionalities and products
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11Developing a Strategic Research Agenda and Roadmap (2)Developing a Strategic Research Agenda and Roadmap (2)
Research & Technology areas in IB• Novel enzymes and microorganisms – metagenomics• Microbial genomics and bioinformatics• Metabolic engineering and modeling• Performance proteins and nanocomposite materials• Biocatalyst function and optimization• Biocatalytic process design• Innovative fermentation science• Innovative down-stream processing• Integrated biorefineries
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Novel biotechnological processes for production of polymers,
chemicals, and biofuels from waste
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BackgroundBackground 13
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Ecological reasons to promote „White Biotechnology“: Global Warming, Green house effect
„Rio Declaration on Environment and Development“ June 1992: Broad consensus to switch to alternative, sustainable Technologies
Principle 4: „In order to achieve sustainable development, environmental protection shall constitute an integral part of the development process and cannot be considered in isolation from it.“
Rising Prices for mineral oil: Economic necessity to promote technologies independent from the availability of fossil feedstocks
Major Drawback for „White Biotechnologie“: Costs for Raw Materials
Solution Strategy: Utilization of Waste Materials for Production of Biopolymers, Biochemicals and Biofuels
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140
130
14June 2008: Price surmounted 130 US-$ per barrel
July 2008: Price surmounted 140 US-$ per barrel
Need for Need for „„White BiotechnologyWhite Biotechnology““ for Production of for Production of Biopolymers, Biofuels and Biochemicals? Biopolymers, Biofuels and Biochemicals?
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„Target Areas“: Final Products from Conversion of Waste Materials via „White Biotechnology“
Major substrates for production of biopolymers, biofuels and biochemicals:
Monosaccharides: Glucose, Galactose, Fructose, Xylose,
Arabinose
Disaccharides: Sucrose, Lactose, Maltose, Cellobiose
Polysaccharides: Starch, Cellulose, Lignocellulose
Organic acids
Lipids
Alkohols: Glycerol, Methanol
Industrial producers of Waste streams:
Proteinaceous materials (Peptides)
Biodiesel production: raw glycerol phase, low-quality biodiesel fractions
Dairy Industry: Whey
Wood processing industry,
Paper Industry
Additional agricultural branches (e.g. straw from rice, mais etc., olive oil production, palm oil industry, sugar beet industry)
Slaughterhouses and Rendering Industry: Meat- and Bone Meal, slaughter wastes
Biochemicals(Fine chemicals, Organic acids,
Antibiotics, Aromatics, Surfactants, Solvents,
Chiral Synthons)
Biofuels(Bioethanol, Biodiesel)
Biopolymers(PHA, PLA)
Catalytically active Biomass for Production of Biopolymers, Biofuels
and Biochemicals
Sugar cane industry: Molasses, Bagasse
Final Products:
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Brazil: Integration of Biofuel & Biopolymer Production into Sugar Cane Industry: Actual and Potential Utilization of the waste streams
Sugar Cane
Milling
Extraction
Raw Juice
Crystallization
Molasses
Saccharose
Steam and electrical power
CombustionBagasse
Hydrolysis to Glucose and Fructose
Convertible Sugars (Glucose, Xylose, Arabinose)
PHA Biopolymer Production
Fermentative Conversion to
Bioethanol1.) Production of catalytically active Biomass
2.) Production of PHA biopolyesters
Hydrolysis
Biofuel Production
Destillation
Bioethanol
Higher Alcohols (Butanol, Pentanols)
PHA Biopolymers
Downstream Processing:
Extraction of PHA from biomass
Residual BiomassHydrolysis
to peptides and amino acids
Selection of production strain!
Fibers potential filler for PHA-based materials?!
Extraction solvents!
180.000 t/a
30.000 t/a
10.000 t/a
561.600 t/a
32,4 GW/h / a
395.000 t steam/ a
52.575 m3/a2,160.000 t/a
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PHB INDUSTRIAL S/A – Sao Paulo, Brazil
View of the PHB Pilot Plant for 50 t/a
Production strain: Cupriavidus necator DSM 545 (formerly Wautersia eutropha)
Intented industrial scale production of PHA: 10.000 t/a
Production of PHB homopolyester and Poly-3-HB-co-3HV copolyesters from sugar cane saccharose; autarkic energy supply!
Basic research: TU Graz, Austria
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Whey from Dairy Industry – a versatile Feedstock for Biotechnology
Application of Whey lactose (D-gluco-pyranose-4-ß-D-galactopyranoside) from dairy industry: animal feed, sweets, food processing, baby food, laxatives, pharmaceutical matrices
But: annually 13,500.000 t of Surplus Whey in Europe (620.000 t lactose)!
Ecological problem; polluting whey partly disposed in sea
2001: EU – project WHEYPOL (G5RD-CT-2001-00591): application of surplus whey from Italian dairy industry as substrate for PHA biopolyester production
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From Milk to Whey towards PHA Biopolyesters
Pasteurization
Transformation (enzymatic or acidic)
Skimming
Full Fat Whey
Pasterization
Concentration
WHEY CONCENTRATE
Ultrafiltration
Whey Whey PermeatePermeate
Whey Retentate
Curd cheese
Desalting ?!
(necessity depends on production strain)
α-Lactoglobulin (2 wt.-%), ß-Lactoglobuline (9 wt.-%); Lactose (15 wt.-%)
20 – 21 wt.-% Lactose (81% of the entire lactose from milk)
(ca. 620 000 t/a in EU from surplus whey!)
Skimmed Whey (ca. 13 500 000 t/a in EU surplus!)
(ca. 2 700 000 t/a in EU surplus!)
Storage
Storage
MILK
Lactose Hydrolysis to Glucose and Galactose ?!
(depends on production strain)
1.) Production of catalytically active Biomass
2.) Production of PHA biopolyesters
Yield PHA/C-source = 0,33 g/g: ca. 200 000 t/a PHA200 000 t/a PHA in EU from surplus whey possible!!
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Different Routes from Whey Lactose to Biopolyesters (Koller et al., 2007)
Whey Lactose
Hydrolysis towards Glucose and Galactose for Production of PHA
Direct Application of Lactose (sufficient ß-Galactosidase activity of production strain) for production of PHA
Bioconversion 1: via Lactobacilli from Lactose to Lactic Acid
Bioconversion 2: from Lactate to PHAPolylactic acid
(PLA)(www.igb.frauenhofer.de/WWW/GF/dt/GFDP 21 Molke.dt.html)
Conversion to Lactic acid esters → Green Solvents
Pyrolysis
Unsaturated compounds (Crotonic acid, 2-Pentenoic acid etc.) Synthons for chemical synthesis
Lactones
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Alternative Biotechnological Products from Whey Lactose
Bioethanol: Golden Cheese Company, California (19.000 m³ Bioethanol/year) (For Europe: Surplus whey would yield 290.000 m³ Bioethanol/year) (www.ethanolfra.org/pr010201.html)
Antibiotics: e.g. Bacteriocin Nisin (polycyclic peptide antibiotic from Lactococcus lactis) against highly pathogenic food-spoiling bacteria Listeria monocytogenes and Clostridium botulinum (Hickmann, Flores, Monte Alegre, 2001)
Sophorolipids: Emulsifiers and Surfactants for pharmaceutical, cosmetic and food industry; chemically: sophorose derivates linked to hydroxy fatty acids Two –step process: Yeast Cryptococcus curvatus cultivated on
whey permeate, accumulates single-cell-oil (SCO) from whey lactose. SCO is converted in a second step to sophorolipids by Candida bombicola (Daniel et al., 1999))
www.lipidlibrary.co.uk/Lipids/rhamno/image006.gif www.profoodinternational.com
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The Increasing Amounts of Biodiesel
Legislative Situation by the European Commission: Shares of Biofuels [%]:2005: 2%2010: 5,75%possibly up to 20% until 2020 (8 * 1010 Liter/a in Europe)
2005: Production of 1,925.000 t in Europe (= 192.500 t glycerol)
2008: 2,649.000 t in Europe (= 264.900 t glycerol) Austria: 2006 Production of 121.665 t Biodiesel; 2007:
241.381 t (+98%!!!)
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Glycerol Liquid Phase: Waste from the Biofuel Production for the Production of Biopolymers
WASTE LIPIDS
MeOH (EtOH) OH-
Transesterification
Mixture Biodiesel -Glycerolphase
Separation
Washing, Dewatering
BIODIESEL (RME)
GLYCEROL LIQUID PHASE (GLP)
Degreasing
Demethanolization
1.) Production of catalytically active Biomass
2.) Production of PHA biopolyesters
Yield PHA/C-source = 0,33 g/g: ca. 88 000 t/a PHA88 000 t/a PHA in EU from surplus GLP possible!!
Biotechnological Production of PHA Biopolyesters
Downstream Processing
PHA Biopolyesters
Residual Biomass (Proteins, Lipids)
e.g. Waste Cooking Oils, waste animal fats
typically 2-4 wt.-% of biomass
Some lipids: direct application as feedstock!
Low-quality biodiesel fractions: excellent feedstock for PHA
production!
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Lignocellulosic Feedstocks
Occurence of lignocellulosic waste: wood residues (including sawmill and paper mill discards) municipal paper waste agricultural residues (including corn stover, rice straw and sugarcane bagasse) special energy crops
Amounts: non-wood lignocellulosic straw alone is estimated with 2,5*109 t/a Composition of Lignocellulose:
Carbohydrates Lignin (Methoxyphenylpropane)
Cellulose fraction Hemicellulose fraction
Monomer: Glucose (Hexose) Monomers: Xylose, Arabinose (Pentoses)
+
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Biotechnological Utilization of Lignocellulose Obstacle: Lignocellulose has evolved to resist
degradation and to confer hydrolytic stability and structural robustness to the plant cell walls by crosslinking between the carbohydrates and the lignin via ester and ether linkages
Focus of research: UPSTREAM TECHNOLOGY: Enhanced lignocellulose digestion and the development of EFFECTIVE ENZYMES for the degradation of cellulose and hemicellulose into glucose and pentoses are the prerequisite for an efficient production of the desired bio-products
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Composition of Different Lignocellulosic Materials
Cellulose [wt.-%]
Hemicellulose [wt.-%]
Lignin[wt.-%]
Corn cobs 42 – 45 33 – 35 10 - 15
Corn stover 35 25 - 38 35
Wheat straw 33 - 47 22 – 30 13 - 19
Hemp straw 44 - 45 19 - 21 20 - 22
Rice straw 39 36 10
Bagasse 40 29 13
Beech wood 46 31 23
Fir wood 43 27 29
Poplar wood 50 31 17
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Conversion of Lignocellulose to Value-added Bioproducts
Plant Biomass
Steam Explosion
Extraction with water
Alkaline extraction
Cellulose
Hydrolysis (enzymatic or chemical)
Glucose
EnergyAdhesives
Lignin
Hemicellulose
Pentoses (Xylose, Arabinose)
High energy input needed!
Alternatives have to be developed!
e.g.: Solid State
Fermentation!
Hydrolysis (enzymatic or chemical)
Biotechnological Production
of Biopolyesters
Development of efficient hydrolysis methods required!!
Fermentation to Bioethanol
Petschacher Barbara, Diploma Thesis, Graz University of Technology, 2001
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Follow-up Products of PHAs: Chiral Synthons for Organic Synthesis
Chiral synthons: Stereoregular compounds acting as chiral precursors, e.g. production of pharmaceuticals, pheromons, vitamins, antibiotics, aromatics, perfumes
PHAs: Biobased Polyesters consisting mainly of optically pure monomers Chiral center
Hydrolysis leads to a rich source of bifunctionel, R(-)-configurated hydroxy acids.
Market value higher than for the polymer itself!
Classical Hydrolysis:
Isolation of PHA
PHA
acidic alcoholysis of the isolated PHA
Optically pure monomers
(Seebach et al., 1992; Seebach and Züger, 1982)
In-vivo degradation of PHA by adjusting the enzymatic systems involved in intracellular PHA metabolism via the cultivation conditions (C-source, pH, T); excretion of metabolites
Highly efficient process!
App. 130 PHA buliding blocks reported- broad range of possible chiral synthons
(Lee et al., 1999)Process rather complex and highly Solvent-demanding!
In-vivo degradation
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Meat- and Bone Meal (MBM) from Slaughterhause Waste & Rendering Industry – a Precious Nitrogen Source for Biotechnological Purposes
Classical Utilization of MBM: Animal Feed Problem: The emerge of Bovine Spongiform
Encephalopathy (BSE, „Mad Cow Desease“) Peak: Infection of 3500 head of caddle weekly in
Great Britain Alternative Utilization: Energy production by
Combustion → low value-creation 2001: Task Force Graz University of
Technology for Safe Utilization of MBM to produce value-added products!
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Hydrolysis of Meat- and Bone Meal
Precondition of Safe Utilization of MBM: Hydrolysis of MBM to destroy prions
Structure of a Prion
Causing BSE SDS-Gel-Electrophoresis of alkaline Hydrolysis of MBMSDS-Gel-Electrophoresis of alkaline Hydrolysis of MBM
(PhD thesis José Neto, Graz University of Technology, 2006)(PhD thesis José Neto, Graz University of Technology, 2006)
Hydrolysis time [h]
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Production of Meat- and Bone Meal
Application of hydrolyzed MBM for Biomass production
Possible: Removal of Lipids prior to hydrolysis („Degreasing step“)
Application of lipids for Biodiesel Production or as carbon source for fermentative Production of e.g. Biopolymers
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Concluding Remarks A broad range of waste materials from different origins
exists to be potentially utilized for biotechnological production of biopolymers, biofuels and biochemicals
Selection of the appropriate waste stream for biotechnological purposes depends on the global region where the production is intended. Facilities for production should be integrated into existing production lines, where the waste streams directly accrue (Prime example: Integration of sugar-, bioethanol and biopolymer production in Brazil)
Improvement of upstream technologies, selection of optimized biocatalysts, enhanced downstream processing and autarkic energy supply are required to achieve cost efficiency in the production of biopolymers, biofuels and biochemicals from waste.
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Content :
Limitation and rising prices of fossil feedstocks and the increasing need for „White Biotechnology“: Ecological and Economic needs
„Target Areas“: Final products from conversion of waste materials via „White Biotechnology“
What waste materials are available for biotechnological purposes (occurence and the challenges of their utilization) Meat and Bone Meal (Slaughterhouses and Rendering industry) Sugar Cane industry – Integration of Biofuel and Biopolymer
Production Whey (Dairy Industry) Raw Glycerol Liquid Phase (from Biodiesel Production) Waste Lipids Cellulosic and Lignocellulosic Feedstocks Follow-up Products of PHAs: Chiral Synthons for Organic
Synthesis
Summary
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THANK YOU
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