
BMP testingFats, oils and animal by-products
Vegetable oil (rapeseed, sunflower) — BMP: 4 studies, weighted mean 777 m³ CH₄/t VS
Vegetable oil (rapeseed, sunflower) has a very high energy potential, but is a strong risk of inhibition and foaming. In biogas plants it is used only occasionally and in small doses.
Photo Dr Dobeaucoup / Wikimedia Commons, licence CC BY-SA 4.0, source file; changes: cropping
- Weighted mean
- 777m³ CH₄/t VS
- Range
- 540–940m³ CH₄/t VS
- Records
- 4studies
- Publications
- 2sources
- Temperatures
- 35 °Cof the test
Methane in biogas
High methane content · ≈ 6.3 kWh/m³ of biogas
estimate from the substrate type The collected studies contain no measurement. The interval follows from the approximate composition (carbohydrate-dominated (no protein or fat characteristics); fat-rich (process classification)) and the yields of compound groups according to FNR.
Rating for biogas plants
not rated — editorial rating for biogas plants
Not rated: no dry matter or volatile solids in the data. We calculate the rating when the dry matter and volatile solids of the material are known.
Add to the co-digestion calculator CSV data
BMP curves from 4 studies
Weighted mean Individual records
Dashed lines are a model curve (first-order kinetics, B(t) = B₀·(1 − e−kt)); the end point comes from the publication. All curves are model curves.
Cumulative methane production over the test [m³ CH₄/t VS]. The thick line is the weighted mean of all records (777); dots mark the end values given in the publications. Point at the chart to read values; click a legend item to hide or show a record.
Records and sources
Download CSV| Source | BMP m³ CH₄/t VS | Temperature | Sample | Curve |
|---|---|---|---|---|
| Chynoweth et al. (1993) DOI | 940 | 35 °C · mesophilic | Vegetable oil | end point (model curve) |
| Kouas et al. (2017) · 1 DOI | 540 | 35 °C · mesophilic | oil | end point (model curve) |
| Kouas et al. (2017) · 2 DOI | 611 | 35 °C · mesophilic | oil | end point (model curve) |
| Kouas et al. (2017) · 3 DOI | 691 | 35 °C · mesophilic | sunflower oil | end point (model curve) |
| Weighted mean | 777 | arithmetic mean 696, SD 174 | ||
Process properties
Advantages
- Methane potential in the Substraty.pl BMP dataset: weighted mean 777.0 m³ CH₄/t VS (SD 174.3; 4 records, 2 sources).
- Pure lipid without water and protein - maximum energy concentration in the mix (Long et al. 2012).
- In co-digestion with slurry, lipids are described as increasing yield if the dose is limited (Long et al. 2012).
Drawbacks and risks
- Triacylglycerols give glycerol (readily fermentable) and LCFA - the latter inhibits methanogenesis and leads to biomass flotation and foaming (Long et al. 2012).
- Separates out and forms a layer on the surface - without good mixing an indicator of local overloading (Long et al. 2012).
- Unsaturated acids (oleic, linoleic) are more strongly inhibitory than saturated ones (Elsamadony et al. 2021).
Co-digestion — what to combine it with, what to watch out for
- combines well
substrates: high alkalinity (buffer) — e.g. Cattle manure, Pig slurry, Cattle slurry, Duck slurry, Rumen and digestive tract content
- caution
Glycerol refining residues (MONG, distillation residue)
Glycerine and its residues add readily degradable carbon to the same mix, which increases the risk of overloading.[3][4]
- avoid
substrates: fat-rich — e.g. Food waste, Spent coffee grounds, Primary sludge, Sunflower seeds, Olive pomace / olive mill solid waste
Oil + animal fat/FOG: shared lipid limit, LCFA accumulation.[5][1]
Dosing
No source-based percentage for pure oil. In a study with technical fat and slurry, floating granules formed above 2% of the mixture (Pitk et al. 2014); take this as an upper guide and start an order of magnitude lower.
Introduce gradually, starting with a small dose and monitoring the process (e.g. FOS/TAC, pH, gas composition).
Sources of the process data
- Pitk et al. (2014). Mesophilic co-digestion of dairy manure and lipid rich solid slaughterhouse wastes. Bioresour. Technol.
- Creamer et al. (2010). Stable thermophilic anaerobic digestion of dissolved air flotation (DAF) sludge by co-digestion with swine manure. Bioresour. Technol.
- Fountoulakis, Petousi, Manios (2010). Co-digestion of sewage sludge with glycerol to boost biogas production. Waste Manag.
- Elsamadony et al. (2021). Advances towards understanding long chain fatty acids-induced inhibition and overcoming strategies for efficient anaerobic digestion process. Water Res.
- Long et al. (2012). Anaerobic co-digestion of fat, oil, and grease (FOG): A review of gas production and process limitations. Process Saf. Environ. Prot.
The co-digestion calculator will assess a specific mixture containing this substrate.
What it is and where it comes from
Vegetable oil is a liquid fat produced mainly from rapeseed and sunflower seeds. The compilation includes records for rapeseed oil, sunflower oil (including edible oil) and oil designated generally as vegetable. Pure oil is a product with commercial value, so as a biogas plant substrate it occurs mainly in studies or as a possible waste requiring no processing when the product range changes.
Properties relevant to digestion
Oil consists of triglycerides, which break down into glycerol and long-chain fatty acids (LCFA). Glycerol is readily fermentable, whereas LCFA, especially unsaturated ones, can inhibit methanogenesis, adsorb onto biomass and cause it to float and foam. The dose must therefore be very cautious, gradual and distributed within the mixture. Oil has practically no water or protein and a very high share of organic matter, so it is a concentrated material. It requires good mixing, because it separates as a layer on the surface.
How to read the spread of results
The records concern different oils (rapeseed, sunflower, edible) and come from several studies, including one from 1993. With a pure lipid the result is sensitive to the substrate-to-inoculum ratio: too high a dose in the test causes inhibition and underestimated results, while too low a dose gives a result that mainly reflects the method. Adaptation of the inoculum to fats, the way the oil is emulsified, the length of the test and the conversion to volatile solids also have an effect. The results from different studies are therefore not a simple measure of the material alone.
In biogas plant practice
Vegetable oil is not a standard biogas plant substrate. If it is nevertheless present, it should be at a minimal share of the feed, with monitoring of the volatile fatty acid concentration, pH and the tendency to foam. It requires a heated tank, good mixing and dosing in small portions. The commercial value of the oil usually exceeds the benefit of digesting it, so fatty wastes such as used oil or fats from separators are more realistic. Legal requirements depend on the origin and classification of the material, so they should be checked before use. When testing your own batch, it is recommended to run several BMP tests at different substrate-to-inoculum ratios to establish the threshold at which inhibition appears, and only then to plan the dose at the plant.
Methodology in brief
BMP is the amount of methane obtained from volatile solids (VS) in a batch test, given in m³ CH₄ per tonne of VS (numerically the same as NmL CH₄/g VS in the publications) and converted to normal conditions (0 °C, 101.325 kPa). The weighted mean gives each publication a total weight of 1, split equally between its results for the substrate — a paper testing twenty varieties does not outweigh a paper with a single sample. In inter-laboratory programmes the unit is the laboratory (total weight 1), and within it the weight of a test grows with the number of bottles (replicates). Results after pretreatment (e.g. thermal, chemical, enzymatic) are shown separately and are not included in the mean.
Solid lines are curves measured in the tests. Where a publication gives only the final result, we draw a first-order kinetic model, B(t) = B₀·(1 − e−kt): only the end point comes from the publication, and the shape of the curve serves purely as visualisation — do not read the production on a particular day from it. For this substrate k = 0.091 d−1 was assumed (no kinetic data for the group – the median of all available rate constants k (93 values) was used).
The statistics describe the spread of published results — a descriptive compilation, not a meta-analysis or a guarantee of plant yield.
Bibliography
- Chynoweth, D.; Turick, C.; Owens, J.; Jerger, D.; Peck, M. (1993). Biochemical methane potential of biomass and waste feedstocks. Biomass and Bioenergy 5(1), 95–111. DOI: 10.1016/0961-9534(93)90010-2 DOI
- Kouas, M.; Torrijos, M.; Sousbie, P.; Steyer, J.P.; Sayadi, S.; Harmand, J. (2017). Robust assessment of both biochemical methane potential and degradation kinetics of solid residues in successive batches. Waste Management 70, 59–70. DOI: 10.1016/j.wasman.2017.09.001 DOI
All sources of the site: bibliography.





