
BMP testingBy-products of the agri-food industrysingle study (3 samples)
Coffee husk — BMP: 3 studies, weighted mean 152 m³ CH₄/t VS
Coffee husk is a dry, lignocellulosic waste from the dry processing of coffee cherries; in the dataset it was tested at three temperatures: 21, 30 and 37 °C.
Photo Daniel Case / Wikimedia Commons, licence CC BY-SA 4.0, source file; changes: cropping
- Weighted mean
- 152m³ CH₄/t VS
- Range
- 140–159m³ CH₄/t VS
- Records
- 3single study (3 samples)
- Publications
- 1source
- Temperatures
- 21 °C, 30 °C, 37 °Cof the test
Methane in biogas
Medium methane content · ≈ 5.2 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)) 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 3 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 (152); 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 |
|---|---|---|---|---|
| Chala et al. (2019) · 1 DOI | 140 | 21 °C · psychrophilic | Coffee husk, 21 C | end point (model curve) |
| Chala et al. (2019) · 2 DOI | 157 | 30 °C · mesophilic | Coffee husk, 30 C | end point (model curve) |
| Chala et al. (2019) · 3 DOI | 159 | 37 °C · mesophilic | Coffee husk, 37 C | end point (model curve) |
| Weighted mean | 152 | arithmetic mean 152, SD 11 | ||
Process properties
Low confidence: the description is based on general characteristics of the substrate group, not on studies of this material. Treat it as a hint to be verified.
Advantages
- Methane potential in the Substraty.pl BMP set: weighted mean 152.0 m³ CH₄/t VS (SD 10.6; 3 records, 1 source).
- Dry material, easy to store; contains residual sugars and protein (Hendriks and Zeeman 2009).
Drawbacks and risks
- Caffeine and tannins at a high concentration inhibit microorganisms (Chen et al. 2008).
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
Slurry supplies N and alkalinity, balancing the high C/N of the material.[1][2]
Dosing
No source threshold; low share, combine with slurry.
Introduce gradually, starting with a small dose and monitoring the process (e.g. FOS/TAC, pH, gas composition).
Practical requirements
- Shred: shredding increases the surface available for degradation and speeds it up, but does not necessarily raise the final gas yield (FNR 2010, Ch. 3 “Triturado”).
Sources of the process data
- Hagos et al. (2017). Anaerobic co-digestion process for biogas production: progress, challenges and perspectives. Renew. Sustain. Energy Rev.
- Weiland (2010). Biogas production: current state and perspectives. Appl. Microbiol. Biotechnol.
- Hendriks, Zeeman (2009). Pretreatments to enhance the digestibility of lignocellulosic biomass. Bioresour. Technol.
- Chen, Cheng, Creamer (2008). Inhibition of anaerobic digestion process: A review. Bioresour. Technol.
- FNR (2010). Guía sobre el Biogás – Desde la producción hasta el uso (hiszp. wydanie „Leitfaden Biogas”, GIZ 2013)
The co-digestion calculator will assess a specific mixture containing this substrate.
What it is and where it comes from
Coffee husk arises in the dry processing method, in which whole coffee cherries are dried and the fruit covering is then removed mechanically. It is one of the largest waste streams in coffee-growing countries such as Brazil or Ethiopia. In Poland coffee is imported as beans, so husk does not occur in significant quantities.
Properties relevant to digestion
The husk is a dry lignocellulosic material: it contains cellulose, hemicellulose and lignin, as well as protein, residual sugars, caffeine and tannins. Polyphenols can inhibit microorganisms to some extent, but at typical shares they do not block the process. The structure is fibrous, so hydrolysis is slower than in the pulp and mucilage. The risk of acidification is moderate, and the C/N ratio is relatively high. The material stores well if it is dry.
How to read the spread of results
The dataset contains several records from a single study, carried out at temperatures of 21, 30 and 37 °C. The results are close to one another, which means that within the range studied temperature had little effect on the final result, although it may have affected the rate. The lack of an independent source makes it impossible to assess variability between laboratories. The coffee variety, the degree of comminution, the content of pulp residues, moisture and the inoculum also have an effect.
In biogas plant practice
On coffee farms the husk is sometimes used as fuel, compost or, after treatment, feed, so it competes with biogas. If it goes into the digester, it should be shredded and its share moderate, together with manure or sludge. A low temperature in a hot climate without heating is a realistic scenario for simple installations, which adds practical value to the results at 21 and 30 °C. For installations in Poland the material is of comparative interest only.
On coffee farms, combining the husk with pulp and mucilage, which ferment faster, and with manure is often a good solution. The husk then contributes structure and extends the gas potential, and the sugar fractions ensure a quick start to the process, provided the whole is dosed evenly.
In producing countries the husk is also sometimes sold locally as fuel, which affects its price and availability for biogas installations.
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
- Chala, B.; Oechsner, H.; Müller, J. (2019). Introducing Temperature as Variable Parameter into Kinetic Models for Anaerobic Fermentation of Coffee Husk, Pulp and Mucilage. Applied Sciences 9(3), 412. DOI: 10.3390/app9030412 DOI
All sources of the site: bibliography.





