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  • Biochar
    Important Analysis Methods

Numerous strategies are being implemented to achieve a neutral carbon footprint, but biomass is one of the few alternatives that have the potential to sustainably meet energy and material needs while being, potentially, carbon-negative.

One route for this is by transforming biomass through pyrolysis, a thermochemical modification process where biomass is broken down in an oxygen-free atmosphere into biochar, bio-oil, and combustible gases. Biochar is a carbon-rich material with typically 70 to 80% of fixed carbon (on an ash-free basis) that has a extensive array of potential applications, whereas the combustible gases are commonly used to fuel the pyrolysis process.

During pyrolysis the release of volatiles components present in biomass provides biochar with a characteristic honeycomb structure with, what can be, a relatively high surface area. This porous nature potentially allows biochar to be suitable for a range of applications such as: a soil supplement for improving plant growth; an adsorbent to decontaminate air and water; and as a catalyst during the production of biodiesel.

Additionally, biochar can be used as: a water filter for domestic use; a clean-burning source of bioenergy; an additive for upgrading biogas production; a stabilizer in composting; a carbon sequestration instrument in the building sector; and even for producing engineering parts for electrical devices.

The pyrolysis process is carried out by optimizing parameters such as residence time, temperature, heating rate, inert gas flow rate, and particle size. For example, a particle size of 0.8 mm and a heating rate of 10 °C/min can improve the biochar yield. In contrast, smaller particles and faster heating rates prompts the release of more volatiles, which results in higher bio-oil and gas yields. However, the temperature is considered to be the most critical parameter because this influences biochar porous configuration and yield. For instance, biochar surface area can decrease when the reaction temperature increases (i.e., 400 to 600 °C) due to the melting of its porous structure. Moreover, high temperatures (greater than 400 °C) also lead to thermal cracking, increasing liquid and gas components and decreasing biochar yield

Nevertheless, the most porous biochar is derived from physical or chemical activation using high temperatures (450–900 °C). Physical activation releases volatiles trapped in the biochar pores meaning that the surface area of physically activated biochar is larger and more microporous (less than 2 nm) rather than mesoporous (2–50 nm). Air is one of the most common activation methods because the activation energy is less compared to carbon dioxide or steam, which improves the economics of the process. However, physical activation using air can result in partial combustion, leading to a high ash content and a lower biochar yield if the method is not properly controlled.

During chemical activation biochar reacts with the chosen set of chemicals at temperatures of around 450 to 900 °C. While chemical activation is less common than physical activation, it has several advantages like lower energy input, a better carbon yield, higher microporosity and significantly increased surface area (over 3,000 m2/g). Nevertheless, chemical activation requires regular equipment maintenance because the methods can lead to chemical corrosion.

Important Parameters for Biochar


The key analytes and properties related to biochar, and the analysis packages that Celignis offers for these, are listed below. Click on an a package for further details on it.

Surface Area and Porosity

The surface area of biochar can vary significantly and, with it, the potential range of applications for the biochar. This is because there are numerous variables that can impact the porosity of the sample. These include: the type of feedstock, the pretreatment, process conditions, the presence of ash or condensates clogging the pores, and the selected activation method. Therefore, a sample obtained after pyrolysis-like processes needs to be analysed to determine its surface area and pore size distribution in order to reveal the true porous nature of the sample and its most suitable application.

We determine the surface area and pore size distribution of carbonaceous samples using a Quantachrome NOVA-e Series 2200e analyser which has been designed to satisfy the procedures outlined in EBC (2012-2022) 'European Biochar Certificate - Guidelines for a Sustainable Production of Biochar.' European Biochar Foundation (EBC), Arbaz, Switzerland. Version 10.1 from 10th Jan 2022.

Our analysis packages for surface area and porosity are listed below. Our reports are comprehensive assessments and provide a user-friendly interpretation of the pore analysis results. What´s more, Celignis offers the same quality of data for all the EBC/IBI Analytical Methods, so you can have an exhaustive characterization of your sample. We also provide application tests and consultation services based on the analysis data to enable clients to determine the most suitable application of their biochar samples.

Click here to read in more detail about the techniques we use for surface area and porosity analysis and to see the types of data that our reports provide.

Analysis Packages for Surface Area and Porosity

 

Suitability for Soil Amendment

The amendment of soil with biochar has attrached attention for two main reasons. Firstly, biochar is an inert form of carbon that is highly recalcitrant to microbial degradation, particularly when compared against the feedstocks it has been produced from. Hence, carbon, initially taken from the atmosphere to grow the feedstock used for biochar production, then becomes locked into biochar which is then added to the soil - a form of carbon sequestration.

Additionally, biochar can help improve the fertility of the soils, allowing for enhanced plant growth and resiliance. Biochar can benefit plant growth as a result of several complementary effects including: increasing carbon stocks, increasing nutrient availability, and allowing for an improved environment for Arbuscular mycorrhizal fungi to proliferate. These fungi exist in a symbiotic relationship with plant roots, allowing for the update of increased amounts of nutrients by the plants.

Celignis personnel have prior experience in the evaluation of biochar as a plant growth promoter. Images are provided of a prior nationally-funded research project which looked at the effects of soil amendement using biochars from different feedstocks. It was found that the production over an initial 21 day period was significantly greater than the no-biochar control and that the size of the increase depended on the feedstock from which the biochar was produced. There was also evidence that the plant roots orientated towards the biochar, as shown in the photos here.

At Celignis we can undertake such plant-growth pot trials and we can measure various important productivity parameters, including Time to Germination, Mean Shoot Length, Shoot Weight and Root Weight. We can also measure a range of other properties relevant to soil amendment, including: Electrical Conductivity, Water Holding Capacity, Cation-Exchange Capacity, Liming, and the contents of 18-different Polyscyclic Aromatic Hydrocarbons (PAHs).

We can also take Scanning Electron Microscopy (SEM) images to evaluate the ultrastructure of the biochar, a useful companion piece of data alongside surface area analysis, to see how suitable the biochar can be as a substrate within which Arbuscular mycorrhizal fungi can proliferate.

Relevant Analysis Packages for Soil Amendment

 

Thermal Properties

Biochar has several advantages as a fuel over the original biomass feedstocks. For example, the carbon and hydrogen contents are greater whilst the oxygen contents are lower, leading to increased calorific values. The loss of highly volatile components during the pyrolysis process also allows for biochar to be a cleaner burning fuel.

Many of Celignis's analysis methods and packages designed to evaluate biomass as a combustion feedstock are also relevant for biochar. Click here to read more about these methods.

Additionally, there are number of other analyses that may be of particular interest for biochars. These include the determination of the inorganic carbon content, the ash content at 815 °C (compared with the 550 °C traditionally used for biomass), the inherent moisture content and the thermogravimetric analysis (TGA) of the sample. An example TGA thermogram and differential thermogram are provided in the interactive image displayed here. Click here to read more about TGA analysis at Celignis.


Relevant Analysis Packages for Biochar Thermal Properties

 

Additional Information on Biochar Analysis

Feel free to get in touch with us if you have any questions about our analysis methods for biochar. Relevant members of the Celignis biochar team will be happy to assist. Those team members with the most experience in biochar analysis analyses are listed below.

Sajna KV

Bioanalysis Developer

PhD

<p style="text-align: left;">Our Biomass Detective! Designs, tests, optimizes and validates robust analytical methods for properties of relevance to the various biochar market applications.</p>

Dan Hayes

Celignis CEO And Founder

PhD (Analytical Chemistry)

<p style="text-align: left;">Dreamer and achiever. Took Celignis from a concept in a research project to being the bioeconomy's premier provider of analytical and bioprocessing expertise.</p>



Other Celignis Tests and Services for Biochar

Global Recognition as Biomass and Biochar Experts

Celignis provides valued services to over 1000 clients. We understand how the focus of biochar projects can differ between countries and have advised a global network of clients. We also have customs-exemptions for samples sent to us allowing us to quickly get to work no matter where our clients are based.

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Feedstock Evaluation

Our analysis packages can screen biochar feedstocks. We can estimate biochar yield and quality using feedstock chemical composition and can estimate biochar composition using the ultimate and major/minor elements analyses of the feedstock. With TGA analysis we can also monitor feedstock behaviour under pyrolysis conditions.

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Biochar Production

We can produce biochar samples from your feedstocks using a wide range of temperatures, heating rates, and residence times. We can formulate a Design of Experiments (DoE) to study the effects of varying process parameters on biochar yield and quality and can optimise these outputs according to your desired biochar market applications.

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Biochar Combustion Properties

Biochar can be a superior fuel versus virgin biomass due to its greater carbon content and energy density. We offer a wide array of analysis packages to fully evaluate biochar as a fuel. For example, we can determine both organic and inorganic carbon and can monitor the behaviour of the biochar ash over wide temperature ranges.

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Soil Amendment & Plant Growth Trials

We can test biochar for several properties (e.g. water holding capacity, electrical conductivity etc.) relevant to its use in soil amendment. We can also grow plants in biochar-amended soils and assess the impacts of this approach on germination, plant growth, plant health, and soil biology.

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Analysis of PAHs in Biochar

Polycyclic aromatic hydrocarbons can be formed during the pyrolysis of biomass and accumulate in biochar, leading to potential risks to the environment. We can accurately quantify a range of different PAHs and determine if their concentrations exceed regulatory limits. We can also develop strategies to reduce the amount of PAHs in biochar.

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Surface Area and Porosity of Biochar

The suitable markets for a biochar are often greatly dependent on its surface area and pore size-distrubtion. We provide detailed reports on biochar surface area and porosity and can provide guidance on the implications of the results. We can also work on strategies to increase the surface area and modify the pore-size distribution of biochar.

Further Info...




Thermogravimetric Analysis of Biochar

TGA is a powerful analytical technique for the study of biochars because it allows us to examine the thermal stability of the material as a function of temperature. The thermal stability of biochars is an important factor to consider when evaluating their potential use as a soil amendment or for carbon sequestration.

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Biochar Upgrading

There are several different methods (covering physical, chemical and biologial routes) by which we can upgrade your biochar in order to increase its value and make it more suitable for the desired market applications. We are able to fully characterise the changes in physicochemical properties associated with upgrading.

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Biochar for Carbon Sequestration

Biochar's efficacy as a means for sequestering carbon depends on a range of factors (e.g. feedstock and pyrolysis conditions). We can undertake a range of analytical tests to help you determine the stability of your biochar's carbon. We can also suggest alternative approaches to improve carbon sequestration potential.

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Technoeconomic Analyses of Biochar Projects

Our TEA experts work with you to evaluate the economic prospects of your biochar facility, considering various scale, technology, and feedstock options. We apply accurate costing models to determine CAPEX/OPEX of simulated and pilot scale processes which are then used to determine key economic indicators (e.g. IRR, NPV).

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Research Project Collaborations

Celignis is active in a number of important research projects focused on biomass valorisation. Biochar is a key component in some of these ongoing projects as well as in several prior projects. We are open to participating in future collaborative research projects where our extensive infrastructure and expertise in biochar can be leveraged.

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Publications on Biochar Digestion By The Celignis Team

Abdeldayem, O.M., Dupont, C., Ferrasa, D. and Kennedyab, M. (2025) An experimental and numerical investigation of secondary char formation in hydrothermal carbonization: revealing morphological changes via hydrodynamics, RSC Advances 15: 12723-12738

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Hydrothermal carbonization (HTC) research has mainly focused on primary char production, with limited attention to secondary char, which is formed through polymerization and condensation of dissolved organic compounds in the liquid phase. This research aims to address this gap via an experimental investigation of the impact of stirring on the mass and carbon balance of HTC reaction products, surface functional groups, and surface morphology of secondary char, using fructose as a model compound. A 3D hydrodynamic simulation model was developed for a two-liter HTC stirred reactor. The experimental results indicated that stirring did not significantly influence the pH, mass, carbon balance, and surface functional groups of secondary char produced under the range of experimental conditions (180 C, 10% biomass to water (B/W) ratio, and a residence time of 0-120 min) studied. Nonetheless, it was observed that a stirring rate of 200 rpm influenced the morphology and shape of the secondary char microspheres, leading to a significant increase in their size i.e., from 1-2 um in unstirred conditions compared with 70 um at a stirring rate of 200 rpm. This increase in size was attributed to the aggregation of microspheres into irregular aggregates at stirring rates > 65 rpm and residence times > 1 h. The hydrodynamic model revealed that high turbulence of Re > 104 and velocities > 0.17 m s-1 correlated with regions of secondary char formation, emphasizing their role in particle aggregation. Particle aggregation is significant above a stirring rate of 65 rpm, which corresponds to the onset of turbulent flow in the reactor. Finally, a mechanism is proposed, based on reactor hydrodynamics under stirred conditions, that explains secondary char deposition on the reactor walls and stirrer.

Kwapinska, M., Sommersacher, P., Kienzl, N., Retschitzegger, S., Lagler, J., Horvat, A. and Leahy, J.J. (2024) Release of N-containing compounds during pyrolysis of milk/dairy processing sludge - Experimental results and comparison of measurement techniques, Journal of Analytical and Applied Pyrolysis 178: 106391

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A dried dairy processing sludge (sludge from wastewater treatment of an effluent from a milk processing plant) was pyrolysed in a single-particle reactor at different temperatures from 400 C to 900 C. NH3 and HCN were measured online and offline by means of FTIR as well as by cumulative sampling in impinger bottles (in 0.05 M H2SO4 and 1 M NaOH, respectively) and analysed by photometric method. NO and NO2 were measured online using a nitric oxide analyser while N2O was measured by FTIR. Nitrogen (N) in the sludge and in the remaining char, char-N, was determined. Moreover, tar content in pyrolysis gas was measured and tar-N was determined. The results with respect to N mass balance closure are discussed. The different measurements techniques are compared. For pyrolysis at 520 and 700 nitrogen in the gas phase was mainly contained as N2 (36 % and 40 % respectively), followed by NH3 (15 % and 18 %), tar-N (10 % and 9 %), HCN (1 % and 3 %), NO (1 %) and NO2 (0.2 %). The dairy processing sludge has very specific properties with organic-N present predominantly as proteins and a high content of inherent Ca. These characteristics affected the distribution of N. The amount of char-N was higher while the amount of tar-N lower than for sewage sludge from literature, at comparable pyrolysis temperature.

Kwapinska, M., Pisano, I. and Leahy, J.J. (2023) Hydrothermal carbonization of milk/dairy processing sludge: Fate of plant nutrients, Journal of Environmental Management 345: 118931

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Dairy processing sludge (DPS) is a byproduct generated in wastewater treatment plants located in dairy (milk) processing companies (waste activated sludge). DPS presents challenges in terms of its management (as biosolids) due to its high moisture content, prolonged storage required, uncontrolled nutrient loss and accumulation of certain substances in soil in the proximity of dairy companies. This study investigates the potential of hydrothermal carbonization (HTC) for recovery of nutrients in the form of solid hydrochar (biochar) produced from DPS originating from four different dairy processing companies. The HTC tests were carried out at 160 C, 180 C, 200 C and 220 C, and a residence time of 1h. The elemental properties of hydrochars (biochars), the content of primary and secondary nutrients, as well as contaminants were examined. The transformation of phosphorus in DPS during HTC was investigated. The fraction of plant available phosphorus was determined. The properties of hydrochar (biochar) were compared against the European Union Fertilizing Products Regulation. The findings of this study demonstrate that the content of nutrient in hydrochars (biochars) meet the requirements for organo-mineral fertilizer with nitrogen and phosphorus as the declared nutrients (13.9-26.7%). Further research on plant growth and field tests are needed to fully assess the agronomic potential of HTC hydrochar (biochar).

Kwapinska, M., Pisano, I. and Leahy, J.J. (2023) Preliminary assessment of pyrolysis biochar derived from milk/dairy processing sludge as a potential component of fertilizers, ACS Sustainable Chemistry & Engineering 11(6): 2345-2353

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Disposal of waste-activated sludge [dairy processing sludge, (DPS)] from wastewater treatment plants located in milk processing companies is an increasing concern. DPS is usually applied to farmlands in the vicinity of the dairy companies. This practice is becoming unsustainable due to uncontrolled nutrient loss and potential soil contamination. We propose to recover nutrients in the form of biochar. This paper examines the properties of biochars obtained from slow pyrolysis of DPS. DPS samples were pyrolyzed at laboratory and pilot scale at 600 and 700 C. The elemental properties of biochars, the content of primary and secondary nutrients, as well as contaminants were examined and compared against the European Union Fertilizing Products Regulation. The biochars meet the specified limits for hydrogen-to-organic carbon ratio, chloride, and polycyclic aromatic hydrocarbons intended for gasification and pyrolysis component category materials. In six out of eight biochars, the content of phosphorus (P) as a single declared nutrient and the level of contaminants meet those required for an organo-mineral fertilizer. Only two biochars meet the required concentrations of nitrogen, phosphorus, and potassium. A minimum solid content of 30% in DPS is required to make the process of biochar production energetically sustainable.

Kwapinska, M., Horvat, A., Agar, D.A. and Leahy, J.J. (2021) Energy recovery through co-pyrolysis of wastewater sludge and forest residues-the transition from laboratory to pilot scale, Journal of Analytical and Applied Pyrolysis 158: 105283

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Anaerobically digested sewage sludge mixed with forest residues was pyrolysed at 800 C, at laboratory and pilot scale. The study quantified differences in char and gas yields for tests carried out in a simple fixed bed laboratory reactor and rotating retort pyrolyser at pilot scale, when the residence time of feedstock was 10 min in both cases. The yield of char from pilot scale was 4 % lower than from laboratory scale while the yield of gas was 15.7 % higher. During the pilot scale pyrolysis of anaerobically digested sewage sludge blended with forest residues the gas quality for energy recovery applications was assessed and the fate of impurities (tar, NH3 and H2S) was investigated. The raw pyrolysis gas contained 14.6 g/Nm3 of tar, 36.9 g/Nm3 of NH3 and 793 ppm of H2S. Sixteen N-containing tar species were identified of which pyridine, propenenitrile, 2-methyl-, benzonitrile, and indole are found to be the most abundant. The yield of N-containing tar compounds accounted for approx. 12 % of total tar content. Conditioned pyrolysis gas contained 7.1 g/Nm3 of tar, 0.036 g/Nm3 of NH3 and 119 ppm of H2S. Benzene was by far the most abundant tar compound followed by toluene and styrene. The specifications of the used internal combustion engine were exceeded due to the sum of tar compounds such as fluorantrene and pyrene with 4+ aromatic rings (at 0.0015 g/Nm3) and NH3 content The effectiveness and sustainability of energy recovery in wastewater treatment can be improved using forest industry by-products.

Kozyatnyk, I., Oesterle, P., Wurzer, C., Masek, O. and Jansson (2021) Removal of contaminants of emerging concern from multicomponent systems using carbon dioxide activated biochar from lignocellulosic feedstock, Bioresource Technology 340: 125561

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Adsorption of six contaminants of emerging concern (CECs) - caffeine, chloramphenicol, carbamazepine, bisphenol A, diclofenac, and triclosan - from a multicomponent solution was studied using activated biochars obtained from three lignocellulosic feedstocks: wheat straw, softwood, and peach stones. Structural parameters related to the porosity and ash content of activated biochar and the hydrophobic properties of the CECs were found to influence the adsorption efficiency. For straw and softwood biochar, activation resulted in a more developed mesoporosity, whereas activation of peach stone biochar increased only the microporosity. The most hydrophilic CECs studied, caffeine and chloramphenicol, displayed the highest adsorption (22.8 and 11.3 mg g-1) onto activated wheat straw biochar which had the highest ash content of the studied adsorbents (20 wt%). Adsorption of bisphenol A and triclosan, both relatively hydrophobic substances, was highest (31.6 and 30.2 mg g-1) onto activated biochar from softwood, which displayed a well-developed mesoporosity and low ash content.

Wurzer, C. and Masek, O. (2021) Feedstock doping using iron rich waste increases the pyrolysis gas yield and adsorption performance of magnetic biochar for emerging contaminants, Bioresource Technology 321: 124473

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Magnetic carbons can significantly lower the costs of wastewater treatment due to easy separation of the adsorbent. However, current production techniques often involve the use of chlorinated or sulfonated Fe precursors with an inherent potential for secondary pollution. In this study, ochre, an iron-rich waste stream was investigated as a sustainable Fe source to produce magnetic activated biochar from two agricultural feedstocks, softwood and wheat straw. Fe doping resulted in significant shifts in pyrolysis yield distribution with increased gas yields (+50%) and gas energy content (+40%) lowering the energy costs for production. Physical activation transformed ochre to magnetite/maghemite resulting in activated magnetic biochars and led to a 4-fold increase in the adsorption capacities for two common micropollutants - caffeine and fluconazole. The results show that Fe doping not only benefits the adsorbent properties but also the production process, leading the way to sustainable carbon adsorbents.

Kwapinska, M., Horvat, A., Liu, Y. and Leahy, J.J. (2020) Pilot scale pyrolysis of activated sludge waste from milk processing factory, Waste and Biomass Valorization 11(6): 2887-2903

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The majority of the sludge from the treatment of wastewater in milk processing plants is land spread. The drawbacks of land spreading include local oversupply due to high transport costs, which results in sludge being spread on lands in the vicinity of the dairy factories. Local oversupply can lead to accumulation of certain substances in soil through annual application over many years. Therefore, in the long term, there is a need for alternative methods to recover energy and nutrients from increasing volumes of sludge generated from dairy processing. Pyrolysis offers a potential alternative to land spreading, which can reduce health and environmental risks, while providing an avenue for the recovery of energy and nutrients. Pyrolysis allows energy recovery in the form of a high calorific value pyrolysis gas and a char which may be used as a soil amendment. In this study pyrolysis of dried dairy sludge was carried out at pilot scale. The results indicate that a dried biological sludge can be successfully pyrolysed and when mixed with wood the resulting char meets European Biochar Certificate criteria regarding carbon content. Most of the initial energy content of the feedstock was retained in the pyrolysis gas prior to cleaning, 53%, compared to 34.5% in the char and 1.5% in the tar. For the pyrolysis gas after cleaning (mainly cracking in presence of air) the initial energy content of the feedstock retained in the gas was only slightly higher than that retained in the char, 39.2% versus 34.5%, while the tar accounted for 0.8% of the initial energy content.

Rockwood, D.L., Ellis, M.F., Liu, R., Zhao, F., Ji, P., Zhu, Z., Fabbro, K.W., He, Z. and Cave, R.D. (2019) Short rotation eucalypts: opportunities for biochar, Forests 10(4): 314

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Eucalypts can be very productive when intensively grown as short rotation woody crops (SRWC) for bioproducts. In Florida, USA, a fertilized, herbicided, and irrigated cultivar planted at 2471 trees/ha could produce over 58 green mt/ha/year in 3.7 years, and at 2071 trees/ha, its net present value (NPV) exceeded $750/ha at a 6% discount rate and stumpage price of $11.02/green mt. The same cultivar grown less intensively at three planting densities had the highest stand basal area at the highest density through 41 months, although individual tree diameter at breast height (DBH) was the smallest. In combination with an organic fertilizer, biochar improved soil properties, tree leaf nutrients, and tree growth within 11 months of application. Biochar produced from Eucalyptus and other species is a useful soil amendment that, especially in combination with an organic fertilizer, could improve soil physical and chemical properties and increase nutrient availability to enhance Eucalyptus tree nutrition and growth on soils. Eucalypts produce numerous naturally occurring bioproducts and are suitable feedstocks for many other biochemically or thermochemically derived bioproducts that could enhance the value of SRWCs.



Publications on Thermal Analyses By The Celignis Team

Rashama, C., Kuttuvan, S., V., Gottumukkala, L., Katjouanga, U., Dobkowski, P., Shiwombolo, J., Hilma, N., Bewer, B., Ben, M., Hayes, D., Wakefield, D. (2025) Preliminary evaluation of biofuel production potentials for Southern Africa's encroacher and invasive bush biomass, Bioresource Technology Reports 31: 102251

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The biofuel production potentials for encroacher and invasive bush biomass species found in Southern Africa were assessed using different valorization routes. Theoretical models were employed to calculate the biofuel yields. The gasification-catalytic route produced highest ethanol yields (450–488 L/t) while the lowest values were from enzymatic/acid hydrolysis-to-fermentation route. Blue gum gave the highest ethanol yields. Biodiesel and naphtha yields produced through Fischer-Tropsch synthesis were highest for blue gum (196 L/t) and lowest for Acacia raficiens (176 L/t). The highest biogas and biomethane potential of 458 L/kg.VS and 229 L/kg.VS respectively were obtained from black wattle while the respective lower values (270 L/kg.VS and 132 L/kg.VS) were recorded for blue gum. Senegalia mellifera gave the highest torrefied biofuel energy and mass yields at 0.92 and 0.97 respectively while black wattle had the lowest mass and energy yields at 0.75 and 0.83 respectively. From an energy yield basis, the acid hydrolysis-fermentation route yielded an average of 3.69 GJ/t of biomass while the highest yields came from the gasification-catalytic conversion route which was 9.7 GJ/t. The average energy yield variations across biomass species ranged 5.11–6.19 GJ/t which is around 30 % of the raw biomass' calorific value. These early results provide insights towards the best pairing of appropriate biomass species and energy conversion route. Further evaluations of these biomass-valorization technology pairing to unpack process efficiencies, cost and kinetics are required using real process experiments instead of using theoretical models. These additional tests should include sustainability assessment to guide future commercialization decisions.



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