BMP testingStraws and crop residues

Barley straw — BMP: 8 studies, weighted mean 238 m³ CH₄/t VS

Barley straw is a readily available lignocellulosic feedstock from agriculture. Hard to degrade, with a high C/N ratio, it requires chopping and nitrogen supplementation in the mix.

rating: goodCH₄ ≈ 52 % (estimate)

Published Updated 3 min readFeedstockData Editorial Team

Photo M J Richardson / Wikimedia Commons, licence CC BY-SA 2.0, source file; changes: cropping

Weighted mean
238m³ CH₄/t VS
Range
189–370m³ CH₄/t VS
Records
8studies
Publications
4sources
Temperatures
38 °C, 40 °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 (protein from total nitrogen (N 1 % DM × 6.25)) and the yields of compound groups according to FNR.

How we calculate it and what the zones mean

Rating for biogas plants

good — editorial rating for biogas plantsStable, usually accepted without a fee

Potential per tonne of fresh matter: very high (203 m³ CH₄/t); no particular threats to stability. Handling costs: fibres, floating layer, slow degradation.

Why? Rating factors

Potential per tonne +3

  • +3potential 203 m³ CH₄/t fresh matter (BMP 238 × DM 90.5 % × VS 94.3 %)

Process stability 0

  • 0no factors

Handling and costs −1

  • −0.5fibres, floating layer — shredding and intensive mixing
  • −0.5slow degradation — long retention time

Total points: 2 · thresholds: ≥ 2.5 very good, ≥ 1 good, below — neutral; negative with cumulative process risk.

Editorial rating per the methodology · confidence of the rating: high · excluding market prices

Add to the co-digestion calculator CSV data

BMP curves from 8 studies

Weighted mean Individual records

BMP curves: Barley strawCumulative methane production over time for 8 records and the weighted mean of 238 m³ CH₄/t VS. 8 of the curves are model curves (first-order kinetics).0100200300400051015202530time [d]m³ CH₄/t VSAmon et al. (2007): 189 m³ CH₄/t VS (model curve)Dinuccio et al. (2010): 229 m³ CH₄/t VS (model curve)Menardo et al. (2012) · 1: 240 m³ CH₄/t VS (model curve)Menardo et al. (2012) · 2: 286 m³ CH₄/t VS (model curve)Menardo et al. (2012) · 3: 339 m³ CH₄/t VS (model curve)Menardo et al. (2012) · 4: 370 m³ CH₄/t VS (model curve)Schumacher et al. (2014) · 1: 224 m³ CH₄/t VS (model curve)Schumacher et al. (2014) · 2: 228 m³ CH₄/t VS (model curve)mean238

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 (238); 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
SourceBMP
m³ CH₄/t VS
TemperatureSampleCurve
Amon et al. (2007) DOI18938 °C · mesophilicBarley Strawend point (model curve)
Dinuccio et al. (2010) DOI22940 °C · mesophilicbarley straw · pretreatment: particle size reduction/sample preparation (MY-D: physical treatment)end point (model curve)
Menardo et al. (2012) · 1 DOI24040 °C · mesophilicBarley Strawend point (model curve)
Menardo et al. (2012) · 2 DOI28640 °C · mesophilicBarley Straw · pretreatment: particle size reduction/sample preparation (MY-D: physical treatment)end point (model curve)
Menardo et al. (2012) · 3 DOI33940 °C · mesophilicBarley Straw · pretreatment: particle size reduction/sample preparation (MY-D: physical treatment)end point (model curve)
Menardo et al. (2012) · 4 DOI37040 °C · mesophilicBarley Straw · pretreatment: particle size reduction/sample preparation (MY-D: physical treatment)end point (model curve)
Schumacher et al. (2014) · 1 DOI22438 °C · mesophilic(orig.: “Barley Straw”): value quoted in a literature reviewend point (model curve)
Schumacher et al. (2014) · 2 DOI22838 °C · mesophilic(orig.: “Barley Straw”): value quoted in a literature reviewend point (model curve)
Weighted mean238arithmetic mean 263, SD 63

Typical composition

Dry matter (DM)
90.5% (range 89.2–90.5)
Volatile solids (VS)
94.3 % DM (range 94.3–97.6)
Nitrogen
1 % DM

Median and range of the determinations reported in the publications behind this substrate's BMP records (read from: MY-D); dry matter: 3 determinations, volatile solids: 3 determinations. Samples were tested dried/air-dry – the DM refers to the material in the test, not to fresh material.

Sources: Dinuccio et al. (2010); Menardo et al. (2012); Schumacher et al. (2014).

The composition of the raw material varies between batches — for plant calculations use an analysis of your own sample. The calculator inserts typical values automatically.

Process properties

  • fibrous
  • slowly degrading
  • carbon-rich
  • low in nitrogen
  • forms a floating layer
  • high dry matter
  • editorial classification

Advantages

  • Methane potential in the database: weighted mean 238 m³ CH₄/t VS (median 234; range 189–370; 8 records from 4 sources).

Drawbacks and risks

  • Lignin limits conversion; long HRT (review by Hendriks 2009).
  • Spread of results in the database: standard deviation 63 at a mean of 263 m³ CH₄/t VS (8 records from 4 sources).

Co-digestion — what to combine it with, what to watch out for

Dosing

No source-based dose limits. In practice straw is an additive to a liquid feed; dosing depends on the size reduction and the mixing capability.

Practical requirements

  • Control floating crust and sediment: when solids are fed directly into the digester, the risk of their formation depends on the substrate (FNR 2010, Ch. 3).
  • Size reduction (particles <10 mm improve degradation according to Menardo 2012)

The co-digestion calculator will assess a specific mixture containing this substrate.

What it is and where it comes from

Barley straw is the residue left after the threshing of barley (Hordeum vulgare), grown in Poland for feed and for malt production. After combine harvesting, the straw is spread on the field, baled or ploughed in. It has many uses that compete with a biogas plant: bedding, roughage, organic fertilisation and combustion.

Properties relevant to digestion

Barley straw is a lignocellulosic material with a high dry matter content and low protein content, so it has a very wide C to N ratio. Biological degradation is limited by the lignin-cellulose structure and by the waxy surface of the stalks, which hinders wetting and colonisation by microorganisms. A technological nuisance is floating and scum formation, as well as water absorbency: in a system with a large share of straw, sufficient liquid substrate must be ensured. Chopping increases availability and shortens degradation time, but raises energy consumption.

How to read the spread of results

The dataset contains records from several studies conducted under mesophilic conditions (temperatures ranging from about 38 to 40 °C). The results depend on barley variety, the year and conditions of harvest, straw moisture, degree of chopping (cutting, milling, particle length) and on the substrate-to-inoculum ratio and test length. Because straw kinetics are slow, shorter tests underestimate the result. The dataset covers material without pretreatment; methods such as extrusion, steam or alkaline treatment change the result significantly.

In biogas plant practice

Barley straw is rarely the main substrate. Used in a small share in a mix with slurry or manure, it can increase the dry matter of the feed, but raises the mixing requirements. Chopping and protection against contamination with soil and stones are necessary. Straw should be stored dry, because moisture leads to losses and mould growth. Because of competing uses and the cost of harvesting and transport, profitability must be calculated for the specific location. The energy yield is worth verifying with a BMP test of the batch. It is worth remembering that in a farm's balance straw also has fertiliser and soil-structuring value, so removing all of it is not always advantageous. If a biogas plant uses straw of several species, it is good to record them separately, in order to link changes in yield to the type of feedstock.

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 = 0.136 d−1 was assumed (median of rate constants k reported in the sources and/or fitted to the mean measured curves).

The statistics describe the spread of published results — a descriptive compilation, not a meta-analysis or a guarantee of plant yield.

Full methodology and correction policy

Results after pretreatment (8) — excluded from the mean
SourceBMP
m³ CH₄/t VS
PretreatmentSample
Schumacher et al. (2014)247unspecifiedBarley Straw
Schumacher et al. (2014)242unspecifiedBarley Straw
Schumacher et al. (2014)216unspecifiedBarley Straw
Schumacher et al. (2014)237unspecifiedBarley Straw
Schumacher et al. (2014)251unspecifiedBarley Straw
Schumacher et al. (2014)251unspecifiedBarley Straw
Menardo et al. (2012)340unspecifiedBarley Straw
Menardo et al. (2012)338unspecifiedBarley Straw

Bibliography

  1. Amon, T.; Amon, B.; Kryvoruchko, V.; Machmüller, A.; Hopfner-Sixt, K.; Bodiroza, V.; Hrbek, R.; Friedel, J.; Pötsch, E.; Wagentristl, H.; Schreiner, M.; Zollitsch, W. (2007). Methane production through anaerobic digestion of various energy crops grown in sustainable crop rotations. Bioresource Technology 98(17), 3204–3212. DOI: 10.1016/j.biortech.2006.07.007 DOI
  2. Dinuccio, E.; Balsari, P.; Gioelli, F.; Menardo, S. (2010). Evaluation of the biogas productivity potential of some Italian agro-industrial biomasses. Bioresource Technology 101(10), 3780–3783. DOI: 10.1016/j.biortech.2009.12.113 DOI
  3. Menardo, S.; Airoldi, G.; Balsari, P. (2012). The effect of particle size and thermal pre-treatment on the methane yield of four agricultural by-products. Bioresource Technology 104, 708–714. DOI: 10.1016/j.biortech.2011.10.061 DOI
  4. Schumacher, B.; Wedwitschka, H.; Hofmann, J.; Denysenko, V.; Lorenz, H.; Liebetrau, J. (2014). Disintegration in the biogas sector – Technologies and effects. Bioresource Technology 168, 2–6. DOI: 10.1016/j.biortech.2014.02.027 DOI

All sources of the site: bibliography.