WP 4 – Valorisation of algal biomass

Slides:



Advertisements
Similar presentations
DOE – Products Platform Stage Gate Review Meeting August, 2005 Note: Each presentation is allotted 30 minutes; 20 min. for the presentation and 10 min.
Advertisements

Biorefining – Introduction, Opportunities and Challenges
Heinz-Josef Koch & Ana Gajić
O. Onay, E.Atabay, S.H. Beis and O. M. Kockar Department of Chemical Engineering, Faculty of Engineering Anadolu University, 26470, Eskisehir, Turkey World.
ALGAE: Food for the FUTURE Technology and Innovation for Food Security SYED ISA SYED ALWI Algaetech International, Malaysia.
Hema Rughoonundun Research Week Outline of Presentation The MixAlco Process Introduction Sludge Materials and Methods Results Fermentation of sludge.
What can chemical engineering do for aquaculture R&D?
EXPERIMENT # 9 Instructor: M.Yaqub
Ahmed Atta A Introduction  Algae are a diverse group of primarily aquatic, single celled, plant like organisms. Most algae have characteristics.
European Biomass Industry Association EU BC&E, 25 june 2014, Hamburg, Germany ALGADISK –Novel algae-based solution for CO 2 capture and biomass production.
Chapter 1-3 Concepts of Nutrition. The food components capable of being utilized by animals are described as nutrients. That supports normal reproduction,
An Algal Biofuels Consortium Algae as a Renewable Energy Source: Challenges and Progress Work Funded By US DOE Bioenergy Technology Office, DE-EE
Protein Purification from Corn Germ Danielle McConnell Department of Chemical Engineering Iowa State University.
Extraction and characterization
4.7.2 High-strength Concrete (HSC) Introduction –Definition –Classifications Choice of HSC raw material –Binding material –Excellent aggregate –Superplasticizer.
Ion Exchange for the Production of Cellulosic Ethanol A.Hammervold, C. Cochran, J. Belsher, K. Childress Sponsored by Trillium FiberFuels, Inc. IntroductionProject.
Abstract: The use of renewable energy sources is becoming increasingly necessary to mitigate global warming. Recently much research has been focused on.
Screening of a wide range of pre- treatments for improving the algal biomass solubilization and biogas potential Serge R. Guiot, Caroline Roy and Jean-Claude.
Copyright © by Holt, Rinehart and Winston. All rights reserved. ResourcesChapter menu To View the presentation as a slideshow with effects select “View”
Enzymology Lecture 5 by Rumeza Hanif. Why isolate enzymes? It is important to study enzymes in a simple system (only with small ions, buffer molecules,
Ion-exchange process (softener plant) Water passes through bed of natural zeolite of synthetic resin to remove hardness Calcium (Ca) and magnesium (Mg)
Nutrient recovery from anaerobic co-digestion of Chlorella vulgaris and waste activated sludge Michael Gordon 1, Tyler Radniecki PhD 2, Curtis Lajoie PhD.
S-1007 Multi-State Research Committee
AWAST final meeting - Brussels december 2003 Aid in the management and European comparison of Municipal Solid WASte Treatment methods for a global.
Mobile and Flexible Industrial Processing of Biomass, MOBILE FLIP.
Development of an integrated algal bio-refinery for polysaccharide and bio-fuel production Cesar Moreira 1, Murali Raghavendran 2, Yatin Behl 2, Spyros.
Differentiating Commodity Minerals with Unique Surface Treatments Minerals in Compounding.
Evaluation of a Flowthrough Reactor for Corn Stover Pretreatment Chaogang Liu, Charles E. Wyman Thayer School of Engineering Dartmouth College Hanover,
Sugar Manufacturing Process:
How to Use This Presentation
Technical overview PM2 Stockholm June 2017.
WP 2 – Valorisation of Sludge
Quality Control of Herbal Drug
Wet biomass waste in Europe - Present initiatives and future targets
WP 7 – Integrated Sustainability and Business Viability Assessment
P. M. Follmann, C. Bayer, B. Fischer, M. Wessling, T. Melin
Ioannis Markidis WISE CDT PhD Student, University of Bath
 No fertilisers needed
Third Technical Meeting 13 Sept. Amiens, France
University of Foggia - Italy
BCH 447- Metabolism: Mid term date: Wed 9/2/ /11/2017
Robert H. Narron, Hou-min Chang, Hasan Jameel, Sunkyu Park
Bioenergy from Oilfield Produced Water Hydrothermal Liquefaction
Timeline Roadmap Template
BCH 447- Metabolism: Mid term date: Mon 7/2/ /11/2017
Reporter : Jia-Lin Lu Advisor: Cheng-Ho Chen Date :104/12/22
The Origin of Cells.
Technical meeting Dury, France 13-Sep-2017 Robert Reinhardt
Recovery and Purification of Bio-Products
1Dept. of Entomology and Plant Pathology, Auburn University, AL
Creating a business case for value added algae bio-refining
Seminar on Smolt Production March 1st Campbell River, BC
Results and Discussion
Progress report 7 December 2017
Lab Presentation Preliminary Results
A one-pot procedure for the efficient fractionation and
Project introduction October 2015
Tour of the Cell 11/19/2018.
صدق الله العلي العظيم (سورة النساء:113)
Lab Presentation Preliminary Results
Large-scale laboratory study on the CO2 removal from flue gas in a hybrid adsorptive-membrane installation Krzysztof Warmuzinski, Marek Tanczyk, Manfred.
Hinrich Uellendahl Section for Sustainable Biotechnology
MileStone 2K19, SSBT Coet’s, Department of Chemical Engineering.
Table of Contents – Review of General Properties of Chemistry
Saltgae Workshop Camporosso demonstration site
Saltgae Project 1st Stakeholder Meeting 2nd October 2018
How Lab-Scale Process Optimisation can Lead to Large-Scale Efficiency Improvements Biogas Conference 2018 Berlin, Oct 11th, 2018 Lalitha Gottumukkala
How to Match Feedstock and Technology for Effective Resource Recovery
New solutions to treat dairy wastewater
Presentation transcript:

WP 4 – Valorisation of algal biomass Second Consortium Meeting 13-14 June Stockholm, Sweden

WP4: Valorisation of Algae Biomass Introduction: WP4 WP4: Valorisation of Algae Biomass Biomass Harvesting: IBET Biomass Refinement: Extractis Animal Feed: PMIX Coatings and Adhesives: INSP Fillers and pastes: INSTM/POLIMI

Milestones and Deliverables

Milestones and Deliverables MS5 Optimal pre-concentration by membrane ultrafiltration and low shear centrifugation iBET M16 sept-17 MS6 Choice of the best biomass refinement process Extr M16 sept-17 MS7 Decision on scale up demonstration activities for polymer compounding, pastes and coatings INSTM M23 apr-18 MS8 Valorisation activities: polymer compounding, pastes, coatings and animal feed feedstocks PMIX M36 may-19 Deliverables D4.1 Systems design for harvesting and refinement and algae characterisation iBET M14 jul-17 D4.2 Biomass valorisation report – feasibility Extr M20 jan-18 D4.3 Biomass valorisation progress report – first generation products INSP M28 sept-18 D4.4 Final biomass valorisation report (animal feed, resins and residues) INSTM M36 may-19

iBET

Extractis

Objectives Deliverables Milestones M16 Task 4. 2 Biomass refinement and extraction Objectives Efficiency of the pre-treatment (DM in the sludge around 20%) Fractionate algae biomass into three fractions consisting in respectively oily phase, aqueous phase and sludge with, at least, 80% purity of the oily phase and protein content above 65% of the protein fraction. Purity of beta-carotene (≥ 80%) and digestibility of the protein phase equivalent to soy concentrate. Deliverables D4.2 Biomass valorisation report - Feasibility (M20) Milestones M16 Choice of the best biomass refinement process Verification : - 80% purity of the oily phase - Protein content above 65% - Purity of beta-carotene (≥ 80%).

Description of actions and progress Task 4. 2 Biomass refinement and extraction Description of actions and progress

Task 4.2 Biomass refinement and extraction Last results

Task 4.2 Biomass refinement and extraction Sample Algae Characterizations Yields 7 Archimede Spirulina (HPH +pH11) DM : 98,9% Ash (%/DM) :22.6 Proteins (%/DM) : 35.7 ND 8 Archimede Spirulina (pH4) DM : 99,6% Ash (%/DM) : 3.4 Proteins (%/DM) : 72.2 Solubilisation yield (Prot supernatant 1 / prot algae)= 59% Global yield (prot powder/prot Algae) = 26% 9  Archimede Tetraselmis (HPH+pH11) DM : 99,9% Ash (%/DM) : 16.9 Proteins (%/DM) : 20.6 10  Archimede Tetraselmis (pH4) DM : 99,5% Ash (%/DM) : 4.21 Proteins (%/DM) : 56.2 Solubilisation yield (Prot supernatant 1 / prot algae)= ND Global yield (prot powder/prot Algae) = 40% 2 phases, no lipidic phase Last characterizations in progress : free and total sugars, lipids

Open issues Timing plan Requirements from Task 4.2 Biomass refinement and extraction Open issues Regarding the quantities of lipids requested by PRODUMIX (6kg of lipids which correspond to 300 kg of biomass): at the moment, we are not able to extract lipids. Even if the combination HPH or Ultrasounds pretreatment followed by a chemical treatment is efficient for the proteins extraction, it’s not the case for the lipids. - Will a third approach be necessary? - Will the demo sites be able to provide such fresh quantities to EXTRACTIS? Timing plan - Optimization: - Proteins solubility curves for each algae realized previously - Determination of the best acidic and alcaline pH conditions - Increase the purity of the proteins fraction - Extraction of lipids by optimizing the HPH parameters (number of passes, number of stages…) Requirements from - DEMO SITEs (ARAVA, KOTO and ARCHIMEDE) : algae

PMIX

INSP

INSTM

Introduction: Our role WP4.5: High value material fillers & pastes 4.5a: Algae-residue characterization and modification 4.5b: Development of algae-based biocomposites 4.5c: Development of algae-based 3D-printing of ceramic materials and liquid pastes

Introduction: Chemical process

Microscopy

TGA analysis Spirulina Tetraselmis ~17.0% final weight

Microscopy – Spirulina 5% Pre-heat 2h@ 800°C 50x 100x

Microscopy – Tetraselmis 5% Pre-heat 2h@ 800°C 50x 100x

Mechanical properties

Chemically reactive part Composition Process modifiers Chemically reactive part

Compression Test

Compression Test Empty cylinder samples 3D printed 15 mm 7.5 mm 25 mm

Compression Test – Printed Pipes: time evolution

TGA analysis Spirulina Tetraselmis ~17.0% final weight

Compression Test – Printed Pipes: heating 2h @800h

Ball milling

Compression Test – Printed Pipes: milling 24h milling

Compression Test Milling 24h Printing Heating 800°C

Compression Test – Printed Pipes: heating and milling 2h @800h 24h milling

Next steps

Next steps Start 4.5b: Development of algae-based biocomposites with natural rubber and possibly other polymers Complete the last mechanical tests Validate the results with algae fractions

Thank you for your kind attention