• Analysis of Biochar
    For Use as a Fuel
    At Celignis Biomass Lab

Background

Biochar is produced through the process of pyrolysis, which involves heating biomass in the absence of oxygen. The properties of biochar can vary depending on the feedstock used, the temperature and duration of the pyrolysis process, and other factors.

Biochar can potentially be used in a wide variety of applications, including: as a soil amendment, a component of biobased materials, and in pollution remediation.

Biochar also often has several properties that make suitable as a fuel source. For example, it typically has higher carbon contents and hydrogen contents and lower oxygen contents than the starting feedstock, which result in it having a greater calorific value. Biochar can also usually be compressed at higher densities than the starting feedstock which, coupled with the increased carbon content and calorific values, leads to a fuel with a significantly greater energy density.


The pyrolysis process will also remove the moisture from the feedstock producing a biochar with a very low water content. Furthermore, biochar is typically more stable and resistant to decomposition than the original biomass, which means it can be stored for longer periods of time without losing its fuel properties.

However, it is important to note that not all types of biomass are appropriate for producing biochar suitable for us as a combustible fuel. Factors such as the chemical composition and the content and composition of ash can all affect the properties of the resulting biochar. Additionally, the pyrolysis process itself can impact the quality of the biochar, so careful control of temperature, duration, and other factors is necessary to produce biochar with optimal fuel properties.


Celignis Analyses to Evaluate Biochar as a Fuel

Ultimate Analysis of Biochar


The ultimate analysis of biochar will provide the mass concentrations of the major elements (carbon, oxygen, hydrogen, nitrogen and sulphur) in the sample. The process of pyrolysis typically removes oxygen-containing compounds as non-condensible volatile gases, leaving the resulting biochar with a relatively greater carbon content.

Typically carbon, hydrogen, nitrogen, and sulphur can be determined in the same analytical method and the oxygen content can then be calculated as the remaining mass after the ash content has been considered.

We use an Elementar MACRO Cube unit for the ultimate analysis of samples. It allows for large sample sizes (e.g. around 40mg) to be used than many other elemental analysers, allowing us to improve the precision in the analysis of biochar samples.

Below are listed the Celignis analysis packages that include the ultimate analysis of biochar.



Differentiation Between Inorganic Carbon and Organic Carbon in Biochar

Carbon can be present in both the organic and inorganic form in biochar. Organic carbon refers to carbon that is bound to hydrogen atoms and found in living, or once-living, biomass. Inorganic carbon, on the other hand, refers to carbon that is instead associated with ash cations rather than with the biological polymers of the plant. In biochar, inorganic carbon is typically found as carbonates, e.g. calcium carbonate.

It is important to differentiate between the two forms of carbon in biochar given that organic carbon is preferred when considering biochar as a tool for cabron sequestration, plant growth promotion, and combustion.

The Dumas analysis of a biochar sample, as described in the section above, will provide data on total carbon content of the biochar. However, we can also undertake a carbon analysis of the biochar ash in order to determine the inorganic carbon content. This can then be subtracted from the total carbon content in order to determine the organic carbon content of the biochar sample.


The European Biochar Certificate (EBC), an organisation set up to ensure the quality and safety of biochar produced in Europe, sets an upper threshold of 0.7 for the stoichometric ratio between hydrogen and organic carbon in biochar.

At Celignis we check as to whether the ratio for biochar samples is above or below this threshold value and provide the results in a PASS/FAIL table included as part of our pdf reports. An example table is provided below.



Below are listed the Celignis analysis packages that include the inorganic and organic carbon contents of biochar.



Analysis of the Content and Composition of Ash in Biochar

Ash is generally considered to be the residue remaining after the material has been incinerated. It therefore has no energy value and is therefore of no direct value when considering biochar as a fuel. Indeed, high ash-contents can cause problems in many thermochemical processes (e.g. pyrolysis, gasification, and combustion).

The major cations present in biochar ashes are Calcium, Potassium and Magnesium. Other elements such as Manganese, Sulphur and Phosphorus are present in minor amounts. Trace constituents (such as Al, Fe, Zn, Cu, Ti, Pb, Ni, V, Co, Ag and Mo) are also found in many substrates. The anions that are usually present are Chloride, Carbonate, Sulphate and Silicate.

With biochars produced from waste feedstocks (municipal solid wastes in particular), ashes are often more abundant and more diverse.


At Celignis with our elemental analysis methods we are able to characerise a wide range of major and minor analytes present in biochar ash. Click here to see our relevant analysis packages.

Below are listed the Celignis analysis packages that determine ash composition.



Ash Melting Behaviour of Biochar

Ash melting, also known as ash fusion and ash softening, can lead to slagging, fouling and corrosion in boilers which may reduce conversion efficiency. We can determine the ash melting behaviour of biochar using our Carbolite CAF G5 BIO ash melting furnace. It can record the following temperatures:

Ash Shrinkage Starting Temperature (SST) - This occurs when the area of the test piece of biomass ash falls below 95% of the original test piece area.

Ash Deformation Temperature (DT) - The temperature at which the first signs of rounding of the edges of the test piece occurs due to melting.

Ash Hemisphere Temperature (HT) - When the test piece of biomass ash forms a hemisphere (i.e. the height becomes equal to half the base diameter).

Ash Flow Temperature (FT) - The temperature at which the biomass ash is spread out over the supporting tile in a layer, the height of which is half of the test piece at the hemisphere temperature.



Below are listed the Celignis analysis packages that determine the ash melting behaviour (ash fusion temperature) of biochar.



Calorific Value of Biochar

Calorific value, also known as heating value, is one of the most important properties to consider when evaluating biochar for use as a fuel.

There are several units of measurement. The caloric, or higher heating value (HHV), is independent of moisture content and reliant on the chemical composition of the material. A linear relationship exists between the heat of combustion and the carbon content of the substrate while oxygen, nitrogen and inorganic elements tend to reduce the value.

The Lower Heating Value (LHV), or effective heating value, is perhaps more relevant than the HHV in practical operations. It considers not only the energy required to vaporise the moisture of the biochar but also that necessary to vaporise the water generated when the hydrogen and oxygen elements of the biochar combine. Hydrogen content then becomes a reducing factor in the heating value.

We determine the heating value of biochar directly, by combusting the sample in a bomb calorimeter. Alternatively, it can be indrectly calculated based on the ultimate analysis of the biochar, however these values are less reliable than direct measurements and their accuracies are dependent on the robustness of the mathematical formula to cover different types of biochars.

The heating value can be reported on a dry or wet basis. The wet-basis value considers the moisture content of the biomass and reduces the heating value to incorporate the latent heat of condensation.

At Celignis we use a Parr 6200 bomb calorimeter to directly determine the gross calorific value (higher heating value) of samples. The data from ultimate analysis are then used to calculate the net calorific value (lower heating value).

Below are listed the Celignis analysis packages that determine the calorific value (or heating value) of biochar.



Volatile Matter and Fixed Carbon Contents of Biochar

Fixed carbon refers to the portion of the biochar that remains (excluding ash) after it has been heated to a high temperature (900 oC for a period of 7 minutes). The material that is lost during this treatment is termed the volatile matter. Fixed carbon is a measure of the biochar's carbon content and represents the fraction of the original feedstock material that has been converted into a stable, carbon-rich form during the pyrolysis process.

Fixed carbon is generally considered to be a desirable property of biochar, as it represents a potentially stable form of carbon that can be used for carbon sequestration or soil improvement. The volatile matter content of biochar can affect its physical properties, such as its porosity and density, as well as its chemical properties, such as its ability to release nutrients or affect soil pH. Generally, biochar with a lower volatile matter content is preferred for applications such as soil amendment, as it is less likely to release harmful compounds or affect soil fertility.

In general, fuels with a higher fixed carbon content and a lower volatile matter content are preferred for combustion applications, as they tend to be more efficient and produce fewer emissions. However, the optimal balance between fixed carbon and volatile matter content can vary depending on the specific application and combustion technology being used.

The volatile matter and fixed carbon contents of biochar are generally quite different from those of the starting feedstock material. During the pyrolysis process that produces biochar, the feedstock material is heated to a high temperature in the absence of oxygen, which causes it to decompose and release gases, liquids, and other volatile compounds. As a result, the volatile matter content of biochar is typically much lower than that of the starting feedstock material. For example, wood chips may have a volatile matter content of around 80%, while the volatile matter content of biochar produced from those same wood chips may be only 20-30%.

Correspondingly, the fixed carbon content of biochar is typically much higher than that of the starting feedstock material. This is because during the pyrolysis process, some of the carbon in the feedstock material is converted into a stable form that is resistant to decomposition. This stable carbon makes up the fixed carbon content of the biochar.

Below are listed the Celignis analysis packages that determine the fixed carbon and volatile matter contents of biochar.



Additional Information on Analysis of Biochar as a Fuel

Feel free to get in touch with us if you have any questions about our analytical services for evaluating biochar for use as a fuel. Relevant members of the Celignis biochar team will be happy to assist. Those team members with the most experience with undertaking these tests and interpreting the resulting data 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.

Further Info...




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.

Further Info...




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.

Further Info...




Biochar Analysis

We have an extensive array of analysis packages to evaluate the suitability of biochar for a range of applications. These analyses cover properties relevant to combustion, soil amendment, feed, and biomaterials. Our reports compare the results against internationally-recognised limits for using the biochar in specific end-products.

Further Info...




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.

Further Info...




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.

Further Info...




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.

Further Info...




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.

Further Info...




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.

Further Info...




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).

Further Info...




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.

Further Info...


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

Link

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

Link

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

Link

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

Link

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

Link

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

Link

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

Link

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

Link

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

Link

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 Biochar 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

Link

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

Link

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

Link

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

Link

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

Link

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

Link

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

Link

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

Link

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

Link

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.



...