Production of 1,3-Propanediol Through Fermentation
Background to 1,3-Propanediol Fermentation
Natural microbes that produce 1,3-Propanediol are Klebsiella, Clostridia, Citrobacter, Enterobacter and Lactobacilli. They all use glycerol as a carbon source and produce 1,3 PDO through 3-hydroxypropionaldehyde route
using glycerol dehydratase enzymes and 1,3-propanediol oxidoreductase enzymes. The biggest constraint for microbial production of 1,3 PDO is low yield and productivity which is due to multiple reasons including:
as low cell density, irreversible inhibition of glycerol dehydratase enzyme with glycerol, and requirement of speciality ingredients such as vitamins.
Though the use of waste glycerol from biofuel industry is highly advocated, its usage will cause more complications due to microbial inhibition with the presence of methanol, surfactants, and free fatty acids.
Though the use of waste glycerol from biofuel industry is highly advocated, its usage will cause more complications due to microbial inhibition with the presence of methanol, surfactants, and free fatty acids.
Hence, raw glycerol from industrial streams should be pretreated to remove inhibitors before using it for 1,3-Propanediol or should adapt or isolate the strain to tolerate the inhibitors.
Fermentation strategies should avoid cell toxicity of glycerol and autolysis processes. This can be achieved by following techniques like fed-batch fermentation, sequential fermentation, and immobilised cells. The most suitable downstream technique should be employed for purification of 1,3-PDO in order to make the process economically viable.
Fermentation strategies should avoid cell toxicity of glycerol and autolysis processes. This can be achieved by following techniques like fed-batch fermentation, sequential fermentation, and immobilised cells. The most suitable downstream technique should be employed for purification of 1,3-PDO in order to make the process economically viable.
How Celignis Can Help
At Celignis, we have expertise and experience in performing anaerobic fermentations
and developing fermentation strategies to achieve high cell mass and in situ product recovery techniques. We can screen your feedstock for 1,3-Propanediol production,
adapt the strain to any inhibitors present in the feed, and develop bespoke fermentation and product recovery process.
Our team of experts will innovate with you for you.
Get more info...Get in Touch
Our team of experts will innovate with you for you.
Get more info...Get in Touch
Lactic Acid Fermentation
Lactic acid bacteria are very sensitive and require complex nutrient media compared to other bacillus species that can produce lactic acid.
Hence, industries are constantly looking for fungi and bacillus strains that have low nutrient requirements and can tolerate acidic pH.
At Celignis we have expertise and experience in screening lactic acid bacteria for the selection of substrate- and product-tolerant strains. We can also develop: fed-batch strategies to achieve high cell mass, and in situ product recovery techniques to separate lactic acid from the fermentation broth. We will work with you and develop bespoke lactic acid fermentation methods for your feedstock or industrial waste streams.
Get more info...Lactic Acid Fermentation
At Celignis we have expertise and experience in screening lactic acid bacteria for the selection of substrate- and product-tolerant strains. We can also develop: fed-batch strategies to achieve high cell mass, and in situ product recovery techniques to separate lactic acid from the fermentation broth. We will work with you and develop bespoke lactic acid fermentation methods for your feedstock or industrial waste streams.
Get more info...Lactic Acid Fermentation
Propionic Acid Fermentation
Propionic acid can be produced from a variety of substrates such as glucose, ethanol, lactose, glycerol, and pectin. So, several industrial streams
will be suitable to produce propionic acid, if the bacteria are adapted to the inhibitors present in the waste streams and fermentation is optimised to
achieve high cell densities and high product concentration.
We can perform anaerobic fermentations and develop fermentation strategies to achieve high cell mass and in-situ product recovery techniques. We can screen your feedstock for propionic acid production, adapt the strain to any inhibitors present in the feed, and develop bespoke fermentation and product recovery processes.
Get more info...Propionic Acid Fermentation We can perform anaerobic fermentations and develop fermentation strategies to achieve high cell mass and in-situ product recovery techniques. We can screen your feedstock for propionic acid production, adapt the strain to any inhibitors present in the feed, and develop bespoke fermentation and product recovery processes.
Butyric Acid Fermentation
Butyric acid is biologically produced by Clostridium species and like other acids (acetic acid, lactic acid, propionic acid),
it is toxic to the bacteria after a certain concentration. Hence, the product titres are generally low which makes downstream expensive.
In order to reduce these costs, in situ removal of butyric acid can be developed. In situ removal strategies are not yet industrially applied for butyric acid, but
it is a key area where progress has to be made to make the process economically sustainable.
At Celignis, we have strong expertise in Clostridial fermentation. We can isolate and or adapt the strains that are suitable for your feedstock and can develop fermentation strategies to reduce substrate and product inhibition. We will innovate with you for you.
Get more info...Butyric Acid Fermentation
At Celignis, we have strong expertise in Clostridial fermentation. We can isolate and or adapt the strains that are suitable for your feedstock and can develop fermentation strategies to reduce substrate and product inhibition. We will innovate with you for you.
Get more info...Butyric Acid Fermentation
Butanol Fermentation
Butanol fermentation is also one of the difficult fermentation pathways due to substrate and product inhibition. However, this can be
avoided by fed-batch fermentation and in-situ stripping of butanol. Also, reducing the feedstock and enzyme costs will make the process more
economically viable. Through using industrial waste streams (negative costs), enzymatic cocktails tailored for the feedstock (allowing low-enzyme dosages), and
with high sugar yields, the right choice of microbial strain, and an effective in-situ removal technology, it is possible to develop an economically-viable butanol process.
At Celignis, we have considerable expertise in Clostridial fermentation and especially butanol fermentation. Our Chief Innovation Officer Dr Lalitha Gottumukkala has extensively worked in this area and has isolated novel strains and developed novel methods for non-acetogenic butanol fermentation as part of her PhD.
Get more info...Butanol Fermentation
At Celignis, we have considerable expertise in Clostridial fermentation and especially butanol fermentation. Our Chief Innovation Officer Dr Lalitha Gottumukkala has extensively worked in this area and has isolated novel strains and developed novel methods for non-acetogenic butanol fermentation as part of her PhD.
Get more info...Butanol Fermentation
Polyhydroxy Alkanoates (PHAs) Production
PHA is one of the most complicated fermentation processes, but the possibility to use mixed microbial cultures and the avoidance of sterilisation costs
makes it an interesting process to produce bioplastics. Also, PHA blends are becoming more and more popular to increase the tensile strength and
flexibility of the polymer, possible by using mixed culture substrates.
At Celignis, we have experience in enrichment of desired microorganisms, fed-batch and continuous fermentations with cell-recycling. We can design and develop the most suitable process for your feedstock by using mixed or mono-culture fermentations. We can also develop cost-efficient downstream processing steps for efficient PHA extraction by using non-toxic and environmentally friendly techniques.
Get more info...PHA Production Fermentation
At Celignis, we have experience in enrichment of desired microorganisms, fed-batch and continuous fermentations with cell-recycling. We can design and develop the most suitable process for your feedstock by using mixed or mono-culture fermentations. We can also develop cost-efficient downstream processing steps for efficient PHA extraction by using non-toxic and environmentally friendly techniques.
Get more info...PHA Production Fermentation
Yeast and Fungal Fermentation
Yeast fermentation is one of the oldest fermentations and is used in everyday life to produce a variety of commodity products including bread, beer, wine,
cheese, and soy sauce. A few decades ago, yeast gained popularity as an industrial strain for biorefinery and biofuel applications.
At Celignis, we can use yeast and fungi for the production of: bioethanol, glycerol, single cell oils (SCOs), and emulsifiers, among other products.
Get more info...Yeast and Fungal Fermentation At Celignis, we can use yeast and fungi for the production of: bioethanol, glycerol, single cell oils (SCOs), and emulsifiers, among other products.
Microalgal Fermentation
Algal cultivation is complicated and requires optimisation to achieve high biomass yields. Algal biomass production depends on nutrient uptake and
other environmental conditions such as temperature, pH, salt concentration etc. It is important to select the strain based on the type of
production (open ponds, photobioreactors), feedstock and application. We have particular expertise in the evaluation and optimisation of algae thorugh
our Chief Innovation Officer, Lalitha, who is currently undertaking a Marie-Curie funded project at Celignis on this topic.
Get more info...Microalgae Fermentation 
Contact Us For Further Details
We are available to answer any questions you may have on how to get high value chemicals and biofuels from biomass through fermentation processes.
Just get in touch with us by sending us an email info@celignis.com, giving us a call at (+353) 61 371 725, or through
our contact form.
Get more info...Get in Touch
Get more info...Get in Touch
Special Offer
Analysis Packages
P8 : Lignin Content
Lignin (Klason), Lignin (Acid Soluble), Acid Insoluble Residue, Ash (Acid Insoluble),
Lignin (Klason), Lignin (Acid Soluble), Acid Insoluble Residue, Ash (Acid Insoluble),
P19 : Deluxe Lignocellulose Package
As P10 plus protein-corrected lignin, water-soluble sugars, uronic acids, acetyl content and starch.
As P10 plus protein-corrected lignin, water-soluble sugars, uronic acids, acetyl content and starch.
P15 : Uronic Acids
Glucuronic Acid, Galacturonic Acid, Mannuronic Acid, Guluronic Acid, 4-O-Methyl-D-Glucuronic Acid,
Glucuronic Acid, Galacturonic Acid, Mannuronic Acid, Guluronic Acid, 4-O-Methyl-D-Glucuronic Acid,
P121 : Evaluation of Biomass for Enzymatic Digestibility
Total Sugars in Enzyme Hydrolysate, Glucose in Enzyme Hydrolysate, Xylose in Enzyme Hydrolysate, Arabinose in Enzyme Hydrolysate, Mannose in Enzyme Hydrolysate, Galactose in Enzyme Hydrolysate, Rhamnose in Enzyme Hydrolysate, Cellobiose in Enzyme Hydrolysate, Enzymatic Hydrolysis Kinetics, Cellulose Conversion Yield, Xylan Conversion Yield, Combined Sugar Yield, Cellulose Conversion Rate, Xylan Conversion Rate,
Total Sugars in Enzyme Hydrolysate, Glucose in Enzyme Hydrolysate, Xylose in Enzyme Hydrolysate, Arabinose in Enzyme Hydrolysate, Mannose in Enzyme Hydrolysate, Galactose in Enzyme Hydrolysate, Rhamnose in Enzyme Hydrolysate, Cellobiose in Enzyme Hydrolysate, Enzymatic Hydrolysis Kinetics, Cellulose Conversion Yield, Xylan Conversion Yield, Combined Sugar Yield, Cellulose Conversion Rate, Xylan Conversion Rate,
P122 : Evaluation of Pre-Treatment on Enzymatic Digestibility
As P121 plus comparisons with data from the non-pretreated original sample, including: Increase in Cellulose Accessibility after Pre-Treatment, Percent Increase in Cellulose Conversion Efficiency, Percent Increase in Cellulose Conversion Rate.
As P121 plus comparisons with data from the non-pretreated original sample, including: Increase in Cellulose Accessibility after Pre-Treatment, Percent Increase in Cellulose Conversion Efficiency, Percent Increase in Cellulose Conversion Rate.
P123 : Composition of Residue from Enzymatic Hydrolysis
As P9 but on the solid residue after enzymatic hydrolysis.
As P9 but on the solid residue after enzymatic hydrolysis.
P124 : Fermentation Inhibitors in Enzymatic Hydrolysate
Formic Acid, Acetic Acid, Levulinic Acid, Furfural, Hydroxymethylfurfural,
Formic Acid, Acetic Acid, Levulinic Acid, Furfural, Hydroxymethylfurfural,
P125 : Cellulase Saccharification Efficiency
Includes all hydrolysate sugars and kinetics in P121 and: Cellulose Conversion Yield, Cellulose Conversion Rate
Includes all hydrolysate sugars and kinetics in P121 and: Cellulose Conversion Yield, Cellulose Conversion Rate
P126 : Xylanase Saccharification Efficiency
Includes all hydrolysate sugars and kinetics in P121 and: Xylan Conversion Yield, Xylan Conversion Rate
Includes all hydrolysate sugars and kinetics in P121 and: Xylan Conversion Yield, Xylan Conversion Rate
P127 : Amylase Saccharification Efficiency
Total Sugars in Enzyme Hydrolysate, Glucose in Enzyme Hydrolysate, Maltose in Enzyme Hydrolysate, a-Amylase Hydrolysis Kinetics, Glucoamylase Hydrolysis Kinetics,
Total Sugars in Enzyme Hydrolysate, Glucose in Enzyme Hydrolysate, Maltose in Enzyme Hydrolysate, a-Amylase Hydrolysis Kinetics, Glucoamylase Hydrolysis Kinetics,
P12 : Sugars in Solvent Extract
Glucose, Xylose, Fructose, Sucrose, Mannose, Arabinose, Galactose, Rhamnose, Xylitol, Sorbitol, Trehalose, Mannitol, Arabinitol, Glycerol, Raffinose,
Glucose, Xylose, Fructose, Sucrose, Mannose, Arabinose, Galactose, Rhamnose, Xylitol, Sorbitol, Trehalose, Mannitol, Arabinitol, Glycerol, Raffinose,
P22 : Organic Acids and Furans
Levulinic Acid, Formic Acid, Hydroxymethylfurfural, Furfural, Acetic Acid, gamma-Valerolactone,
Levulinic Acid, Formic Acid, Hydroxymethylfurfural, Furfural, Acetic Acid, gamma-Valerolactone,
P24 : Dimers and Trimers from Hemicellulose Hydrolysis
Xylobiose, Xylotriose, Arabinobiose, Arabinotriose,
Xylobiose, Xylotriose, Arabinobiose, Arabinotriose,
P71 : Seaweed Carbohydrates
Fucose, Mannitol, Glucose, Xylose, Mannose, Arabinose, Galactose, Rhamnose, Total Sugars, Glucuronic Acid, Galacturonic Acid, Mannuronic Acid, Guluronic Acid,
Fucose, Mannitol, Glucose, Xylose, Mannose, Arabinose, Galactose, Rhamnose, Total Sugars, Glucuronic Acid, Galacturonic Acid, Mannuronic Acid, Guluronic Acid,
P72 : Seaweed Amino Acids
Alanine, Arginine, Aspartic Acid, Cystine, Glutamic Acid, Glycine, Histidine, Isoleucine, Leucine, Lysine, Methionine, Phenylalanine, Proline, Serine, Threonine, Tyrosine, Valine,
Alanine, Arginine, Aspartic Acid, Cystine, Glutamic Acid, Glycine, Histidine, Isoleucine, Leucine, Lysine, Methionine, Phenylalanine, Proline, Serine, Threonine, Tyrosine, Valine,
P36 : Major Elements
Aluminium, Calcium, Iron, Magnesium, Phosphorus, Potassium, Silicon, Sodium, Titanium,
Aluminium, Calcium, Iron, Magnesium, Phosphorus, Potassium, Silicon, Sodium, Titanium,
P150 : Plant Pigments
Chlorophyll-a, Chlorophyll-b, Lutein, beta-Carotene, Neoxanthin, Astaxanthin, Zeaxanthin, Antheraxanthin, Violaxanthin,
Chlorophyll-a, Chlorophyll-b, Lutein, beta-Carotene, Neoxanthin, Astaxanthin, Zeaxanthin, Antheraxanthin, Violaxanthin,
P81 : Biomethane Potential - 14 Days
Biomethane Potential (BMP), Total Biogas Volume, Total Solids, Volatile Solids, pH, Biogas Methane Content, Biogas Carbon Dioxide Content, Biogas Oxygen Content, Biogas Hydrogen Sulphide Content, Biogas Ammonia Content,
Biomethane Potential (BMP), Total Biogas Volume, Total Solids, Volatile Solids, pH, Biogas Methane Content, Biogas Carbon Dioxide Content, Biogas Oxygen Content, Biogas Hydrogen Sulphide Content, Biogas Ammonia Content,
P93 : Feedstock Chemical and Biological Analysis
Total Solids, Volatile Solids, pH, Chemical Oxygen Demand (COD), Biological Oxygen Demand (BOD), Phosphorus, Potassium, Ammonia, Carbon, Hydrogen, Nitrogen, Sulphur,
Total Solids, Volatile Solids, pH, Chemical Oxygen Demand (COD), Biological Oxygen Demand (BOD), Phosphorus, Potassium, Ammonia, Carbon, Hydrogen, Nitrogen, Sulphur,
P61 : Sugars in Bio-Oil Water Extract
Levoglucosan, Cellobiosan, Mannosan, Galactosan, Glucose, Xylose, Mannose, Arabinose, Galactose, Rhamnose, Fucose, Sucrose, Cellobiose, Total Sugars,
Levoglucosan, Cellobiosan, Mannosan, Galactosan, Glucose, Xylose, Mannose, Arabinose, Galactose, Rhamnose, Fucose, Sucrose, Cellobiose, Total Sugars,
P63 : Semi-Volatile Oxygenated Components in Bio-Oil
31 constituents including Phenol, Furfural, Syringol, and Vanillin
31 constituents including Phenol, Furfural, Syringol, and Vanillin
P360 : Specific Surface Area (5-Point BET)
Specific Surface Area (Nitrogen Gas Adsorption), BET Isotherm (5 Point Using Nitrogen),
Specific Surface Area (Nitrogen Gas Adsorption), BET Isotherm (5 Point Using Nitrogen),
P364 : Pore-Size Distribution
Specific Surface Area (Nitrogen Gas Adsorption), BET Isotherm (20 Point Using Carbon Dioxide), Pore Volume, Pore Size Distribution,
Specific Surface Area (Nitrogen Gas Adsorption), BET Isotherm (20 Point Using Carbon Dioxide), Pore Volume, Pore Size Distribution,
P366 : Pore Size Distribution Deluxe
Specific Surface Area (Nitrogen Gas Adsorption), BET Isotherm (40 Point Using Nitrogen), Pore Volume, Pore Size Distribution,
Specific Surface Area (Nitrogen Gas Adsorption), BET Isotherm (40 Point Using Nitrogen), Pore Volume, Pore Size Distribution,
P34 : Calorific Value and Elements
Gross Calorific Value, Net Calorific Value, Ash, Carbon, Hydrogen, Nitrogen, Sulphur, Oxygen,
Gross Calorific Value, Net Calorific Value, Ash, Carbon, Hydrogen, Nitrogen, Sulphur, Oxygen,
P36 : Major Elements
Aluminium, Calcium, Iron, Magnesium, Phosphorus, Potassium, Silicon, Sodium, Titanium,
Aluminium, Calcium, Iron, Magnesium, Phosphorus, Potassium, Silicon, Sodium, Titanium,
P37 : Minor Elements
Antimony, Arsenic, Cadmium, Chromium, Cobalt, Copper, Lead, Manganese, Mercury, Molybdenum, Nickel, Vanadium, Zinc,
Antimony, Arsenic, Cadmium, Chromium, Cobalt, Copper, Lead, Manganese, Mercury, Molybdenum, Nickel, Vanadium, Zinc,
P42 : Ash Melting Behaviour (Reducing Conditions)
Ash Shrinkage Starting Temperature (Reducing), Ash Deformation Temperature (Reducing), Ash Hemisphere Temperature (Reducing), Ash Flow Temperature (Reducing),
Ash Shrinkage Starting Temperature (Reducing), Ash Deformation Temperature (Reducing), Ash Hemisphere Temperature (Reducing), Ash Flow Temperature (Reducing),
P393 : Biochar Thermal Properties Deluxe
Moisture, Ash Content (815C), Carbon, Hydrogen, Nitrogen, Sulphur, Oxygen, Chlorine, Volatile Matter, Fixed Carbon, Aluminium, Calcium, Iron, Magnesium, Phosphorus, Potassium, Silicon, Sodium, Titanium, Gross Calorific Value, Net Calorific Value, Ash Shrinkage Starting Temperature (Reducing), Ash Deformation Temperature (Reducing), Ash Hemisphere Temperature (Reducing), Ash Flow Temperature (Reducing),
Moisture, Ash Content (815C), Carbon, Hydrogen, Nitrogen, Sulphur, Oxygen, Chlorine, Volatile Matter, Fixed Carbon, Aluminium, Calcium, Iron, Magnesium, Phosphorus, Potassium, Silicon, Sodium, Titanium, Gross Calorific Value, Net Calorific Value, Ash Shrinkage Starting Temperature (Reducing), Ash Deformation Temperature (Reducing), Ash Hemisphere Temperature (Reducing), Ash Flow Temperature (Reducing),
P394 : Biochar Thermal Properties Ultimate
As P393 plus inorganic carbon, organic carbon, TGA (under nitrogen and air), and inherent moisture
As P393 plus inorganic carbon, organic carbon, TGA (under nitrogen and air), and inherent moisture
P36 : Major Elements
Aluminium, Calcium, Iron, Magnesium, Phosphorus, Potassium, Silicon, Sodium, Titanium,
Aluminium, Calcium, Iron, Magnesium, Phosphorus, Potassium, Silicon, Sodium, Titanium,
P37 : Minor Elements
Antimony, Arsenic, Cadmium, Chromium, Cobalt, Copper, Lead, Manganese, Mercury, Molybdenum, Nickel, Vanadium, Zinc,
Antimony, Arsenic, Cadmium, Chromium, Cobalt, Copper, Lead, Manganese, Mercury, Molybdenum, Nickel, Vanadium, Zinc,
P384 : Biochar Polycyclic Aromatic Hydrocarbons (PAH)
Acenaphthene, Acenaphthylene, Anthracene, Benz[a]anthracene, Benzo[b]fluoranthene, Benzo[k]fluoranthene, Benzo[ghi]perylene, Benzo[a]pyrene, Chrysene, Dibenz[a,h]anthracene, Fluoranthene, Fluorene, Indeno[1,2,3-cd]pyrene, 1-Methylnaphthalene, 2-Methylnaphthalene, Naphthalene, Phenanthrene, Pyrene,
Acenaphthene, Acenaphthylene, Anthracene, Benz[a]anthracene, Benzo[b]fluoranthene, Benzo[k]fluoranthene, Benzo[ghi]perylene, Benzo[a]pyrene, Chrysene, Dibenz[a,h]anthracene, Fluoranthene, Fluorene, Indeno[1,2,3-cd]pyrene, 1-Methylnaphthalene, 2-Methylnaphthalene, Naphthalene, Phenanthrene, Pyrene,
P388 : Biochar Plant Growth Trials
Time to Germination, Mean Shoot Length (Week 1), Mean Shoot Length (Week 2), Mean Shoot Length (Week 3), Mean Shoot Length (Week 4), Shoot Weight (Week 4), Mean Root Length (Week 4), Root Weight (Week 4),
Time to Germination, Mean Shoot Length (Week 1), Mean Shoot Length (Week 2), Mean Shoot Length (Week 3), Mean Shoot Length (Week 4), Shoot Weight (Week 4), Mean Root Length (Week 4), Root Weight (Week 4),
P397 : Biochar Soil Amendment Ultimate
As Deluxe package plus P383, SEM Imaging (P387) and Plant Growth Trials (P388)
As Deluxe package plus P383, SEM Imaging (P387) and Plant Growth Trials (P388)
P399 : Biochar Complete Evaluation Package
Includes everything from P391 (Physical Properties Ultimate), P394 (Thermal Properties Ultimate), and P397 (Soil Amendment Ultimate)
Includes everything from P391 (Physical Properties Ultimate), P394 (Thermal Properties Ultimate), and P397 (Soil Amendment Ultimate)
P34 : Calorific Value and Elements
Gross Calorific Value, Net Calorific Value, Ash, Carbon, Hydrogen, Nitrogen, Sulphur, Oxygen,
Gross Calorific Value, Net Calorific Value, Ash, Carbon, Hydrogen, Nitrogen, Sulphur, Oxygen,
P36 : Major Elements
Aluminium, Calcium, Iron, Magnesium, Phosphorus, Potassium, Silicon, Sodium, Titanium,
Aluminium, Calcium, Iron, Magnesium, Phosphorus, Potassium, Silicon, Sodium, Titanium,
P37 : Minor Elements
Antimony, Arsenic, Cadmium, Chromium, Cobalt, Copper, Lead, Manganese, Mercury, Molybdenum, Nickel, Vanadium, Zinc,
Antimony, Arsenic, Cadmium, Chromium, Cobalt, Copper, Lead, Manganese, Mercury, Molybdenum, Nickel, Vanadium, Zinc,
P40 : Combustion Package
Volatile Matter, Fixed Carbon, Moisture, Ash, Carbon, Hydrogen, Nitrogen, Sulphur, Oxygen, Gross Calorific Value, Net Calorific Value, Chlorine,
Volatile Matter, Fixed Carbon, Moisture, Ash, Carbon, Hydrogen, Nitrogen, Sulphur, Oxygen, Gross Calorific Value, Net Calorific Value, Chlorine,
P41 : Ash Melting Behaviour (Oxidising Conditions)
Ash Shrinkage Starting Temperature (Oxidising), Ash Deformation Temperature (Oxidising), Ash Hemisphere Temperature (Oxidising), Ash Flow Temperature (Oxidising),
Ash Shrinkage Starting Temperature (Oxidising), Ash Deformation Temperature (Oxidising), Ash Hemisphere Temperature (Oxidising), Ash Flow Temperature (Oxidising),
News
October 11th 2019
We are Hiring! Chief Strategy Officer (CSO) Wanted
We are looking for top-class applicants to catalyse Celignis's growth.
We are looking for someone to join the Celignis team and spearhead our growth and expansion into new markets and territories.
The position has a salary of €69.5k for one year, plus €20k of training and €3.5k in relocation funds.
Please click here for further information on the position and how to apply.
Read...
June 30th 2019
We are Hiring! Innovation Developer Wanted
We are looking for top-class applicants to develop bioprocessing IP at Celignis
We are pleased to announce that we have been selected to be awarded funding, through the Horizon 2020 Innosup Innovation Associate programme, to recruit a top-class person to lead the development of our bioprocess concept into a patentable process and prototype product with clear commercial potential.
The SAPHIRE (Self-Assembling Plant-based Hydrogels Induced by Redox Enzymes) project focuses on the production of environmentally-friendly, 100% plant-based, superior-quality hydrogels for food,
cosmetic and pharmaceutical applications.
The position has a salary of €69.5k for one year, plus €20k of training and €3.5k in relocation funds.
Please click here for further information on the position and how to apply.
Read...
June 4th 2019
Celignis Collaborating with Ibiocat on Biorefinery Solutions
Illinois-based Ibiocat, was founded by Charles Abbas, a leading light for over 40 years in biorefining.
Illinois-based Ibiocat, founded by Charles A. Abbas, and Ireland-based analytical provider Celignis, founded by Dan Hayes, have come together to develop bespoke bioeconomy solutions for clients that are looking to add value to their process residues generated from 1G and 2G ethanol plants.
Click here to read more about this exciting collaboration and here to download a promotional flyer.
Read...
May 28th 2019
We're Hosting a Review Meeting of H2020 Project ENABLING
The 2 day event will see all 16 partners of the ENABLING project discuss the progress to date.
This two-day event will see all 16 project partners discuss the progress made in the first 18 months of our Horizon 2020 project ENABLING and make plans for the activities to be undertaken in the second half of the project.
The focus of the project is on supporting the spreading of best practices and innovation in the provision (production, pre-processing) of biomass for the Bio-Based Industry (BBI).
Click here for more information on ENABLING.
Read...
May 8th 2019
ENABLING Newsletter 4 Released
Details the latests activities and findings of the ENABLING project
We are happy to announce that the 4th newsletter of the ENABLING project has been released.
ENABLING is a coordinating and supporting action funded by the H2020-RUR-2017-1 call of the European Union's Horizon 2020 programme.
The title of the project is an acronym that stands for 'Enhance New Approaches in BioBased Local Innovation Networks for Growth'. The focus of the project is on supporting the spreading of best practices
and innovation in the provision (production, pre-processing) of biomass for the Bio-Based Industry (BBI).
Celignis will play a key role in the project with regards to stressing the importance of biomass composition in terms of evaluating feedstock and technology suitability.
Over the course of the project we will also be contacting a number of stakeholders, both in Ireland and overseas, and will be involved in the organisation of a number of networking events.
Read...