Influence of nutrient composition on methane production from animal manures and co-digestion with maize and glycerine

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Influence of nutrient composition on methane production from animal manures and co-digestion with maize and glycerine Kryvoruchko V. a, Amon T. a, Amon B. a, Gruber L. b,schreiner M. c, Zolitsch W. d, a Division of Agricultural Engineering (ILT), University of Natural Resources and Applied Life Sciences, Peter-Jordan Str. 82, A-1190 Vienna b Federal Research Institute for Agriculture in Alpine Regions (BAL Gumpenstein), A-8952 Irdning c Division of Food Chemistry (DLWT), University of Natural Resources and Applied Life Sciences, Gregor-Mendel Str. 33, A-1190 Vienna d Division of Animal Husbandry (NUWI), University of Natural Resources and Applied Life Sciences, Gregor-Mendel Str. 33, A-1190 Vienna Introduction Biogas production from animal manures and co-digestion of energy crops and agricultural wastes is a very promising option to generate renewable energy in the Ukraine. Biogas plants require a targeted nutrient supply to make optimum use of animal manures, energy crops and agricultural wastes. The research project aimed at finding basic principles and data on the metabolic and energetic turnover during anaerobic digestion of animal manures, energy crops and agricultural wastes in agricultural biogas plants. The influence of animal diet and milk yield on the composition of cattle manure and on the methane yield through anaerobic digestion was investigated. Materials and Methods Substance and energy turnover during anaerobic digestion of cattle manure, energy crops and agricultural wastes were measured in eudiometer batch experiments at 40 C that were conducted according to DIN 38 414 (1985, fig. 1). A detailed methodology description can be taken from AMON ET AL. (2003). The Federal Research Institute for Agriculture in Alpine Regions (BAL Gumpenstein) conducted feeding trials with dairy cows at contrasting milk yields and feeding intensities. The animal diets are listed in table 1. 1

Equilibrium vessel Septum for gas extraction Gas manifold Temperature control Water level controller Digester Magnetic stirrer Water bath Fig 1. Eudiometer batch equipment Table 1. Treatment Diet and milk yield of dairy cows and other cattle that delivered the manure for the digestion experiments Description concentrate [kg DM] hay [kg DM] grass silage [kg DM] maize silage [kg DM] milk yield/ consumption [l day -1 ] Dairy_1 dairy cow 0 5.2 10.4 0 11.2 Dairy_2 dairy cow 0 5.4 6.4 5.8 11.2 Dairy_3 dairy cow 4.6 4.0 4.8 5.2 17.6 Dairy_4 dairy cow 5.8 5.0 10.0 0 16.0 Dairy_5 dairy cow 11.0 3.2 3.8 3.6 29.2 Dairy_6 dairy cow 10.0 3.0 6.2 0 29.2 Ox_1 ox young 0.9 0.8 5.0 0 0 Ox_2 ox old 1.3 1.5 9.0 0 0 Bulls_1 fattening bull 2.3 0 6.5 4.5 0 Bulls_2 fattening bull 1.0 1.0 0 7.0 0 Calf_1 calf young 0.4 1.0 0.5 0.5 max. 8 l Calf_2 calf up to 200kg 1.3 2.0 1.0 1.0 0 Y.Cattle young cattle 0.0 2.0 4.0 0 Heifers heifers 0.4 5.0 3.0 0 0 S.Cow suckler cow 1.0 6.5 6.5 0 0 To explore the influence of co-digestion of glycerine with energy crops and pig manure on the methane yield, a basic mixture (BM) was digested that consisted of 31 % fresh masse (FM) maize silage, 15 % (FM) corn maize and 2

54 % (FM) swine manure. To this basic mixture 3, 6, 8 and 15 % (FM) of glycerine were added. Raw glycerine was supplied by the Energy and Protein Supply Company South Styria (SEEG). The chemical composition of the glycerine was analysed by MITTELBACH (2000). Results and Discussion Dairy cow manure Table 2 gives the nutrient composition of the contrasting dairy cow manures: ph, dry matter (DM), crude protein (XP), crude fibre (XF), cellulose (Cel), hemi-cellulose (HCel), lignin (ADL), crude fat (XL), ash (XA), gross energy (GE). Biogas and methane yield per norm litre of volatile solids are listed as well. Table 2. Composition of dairy cow manures and specific biogas and methane yield composition of dairy cow manure gas yield [g (kg DM) -1 ] [Nl (kg VS) -1 ] treatment ph DM XP XF Cel HCel ADL XL XA GE [MJ] biogas methane Dairy_1 6.95 143.7 162.6 265.9 194.7 144.0 162.1 46.4 157.1 15.8 208.2 136.5 Dairy_2 6.79 128.8 154.3 265.8 227.3 175.9 128.2 34.5 155.0 17.3 213.1 131.8 Dairy_3 6.60 135.0 156.6 310.1 250.8 190.3 124.7 23.8 131.7 14.6 245.8 166.3 Dairy_4 6.60 159.6 150.6 279.5 164.1 187.9 183.3 29.1 162.8 19.3 222.5 143.1 Dairy_5 6.70 148.5 180.2 273.3 161.8 208.7 190.4 28.5 148.4 15.6 238.9 125.5 Dairy_6 6.66 157.3 296.5 248.5 210.1 195.5 121.7 30.3 167.8 16.8 267.7 159.2 The dairy cows of the treatments dairy_1 and dairy_2 had a low milk yield, dairy_3 and dairy_4 had a medium milk yield and dairy_5 and dairy_6 had a high milk yield. In each level of intensity, manures with contrasting crude protein levels were produced. The manures with the higher crude protein levels (dairy_1, 3, and 6) gave higher methane yields during anaerobic digestion. Lignin in the manure reduced the specific methane yield. The higher the feeding intensity and the milk yield, the greater was the reduction in methane yield through an increase in lignin content. Manure of the treatment dairy_3 was received from cows with medium milk yield that were fed a well balanced feeding ration. Forage consisted of hay, grass silage and maize silage. Concentrate was supplemented according to the cows` requirements. Manure of the treatment dairy_3 produced the highest specific methane yield of 166.3 Nl CH 4 (kg VS) -1 (fig. 2). 3

Spec. methane yield [Nl CH4* (kg VS) -1 ] 200 150 100 50 Fig. 2. 0 Cattle manure dairy_1 dairy_2 dairy_3 dairy_4 dairy_5 dairy_6 0 10 20 30 40 50 60 Time (days) Cumulated specific methane yield of dairy manures and regression equations Table 3 gives the nutrient composition of the contrasting cattle manures: ph, dry matter (DM), crude protein (XP), crude fibre (XF), cellulose (Cel), hemicellulose (HCel), lignin (ADL), crude fat (XL), ash (XA), gross energy (GE). Biogas and methane yield per norm litre of volatile solids are listed as well. Table 3. Composition of dairy cow manures and specific biogas and methane yield composition of dairy cow manure gas yield [g (kg DM) -1 ] [Nl (kg VS) -1 ] treatment ph DM XP XF Cel Hcel ADL XL XA GE [MJ] biogas methane Ox_1 6.50 127.84 193.6 219.9 211.5 121.9 119.0 44.5 173.5 18.6 268.6 153.9 Ox_2 7.05 134.12 155.9 230.0 204.7 118.1 143.3 33.2 179.0 16.6 207.0 112.9 Bulls_1 6.59 182.52 181.7 229.3 195.8 191.7 104.4 35.7 197.7 16.1 246.8 138.3 Bulls_2 6.30 174.64 129.6 316.7 288.7 232.6 118.4 23.9 101.9 16.3 192.6 110.4 Calf_1 6.70 203.52 182.8 244.3 216.0 190.5 106.3 35.4 125.3 17.3 208.4 113.4 Calf_2 6.40 184.32 148.8 244.7 223.0 181.3 107.2 37.8 154.0 17.6 230.7 131.4 Y.Catle 6.89 120.52 176.7 215.0 194.0 119.8 130.6 36.7 190.1 15.9 230.9 129.9 Heifers 6.80 150.82 135.5 226.8 215.5 157.6 104.8 32.9 219.5 18.4 297.3 172.2 S.Cow 7.15 162.04 144.9 286.3 193.3 180.3 158.4 36.1 192.1 16.7 167.1 98.7 4

As can be seen from figure 3, the treatment Heifers gave the highest methane yield. The slurry of the treatment Heifers had the highest gross energy (GE) content and the lowest lignin (ADL) content. The highest ADL content was observed with the treatment suckler cow (S.Cow). This was probably the reason for the low biogas and methane yield that was measured from this treatment. The treatments fattening bulls (Ox_2) and young cattle (Y.Cattle) confirm this assumption. Net total methane yield is likely to be limited by the ADL content in animal manures. When the ADL content is low, then the amount of other components as cellulose, crude protein (XP) and crude fat (XL) has a significant influence on the methane yield. 200,0 Spec. methane yield [Nl CH4* (kg VS) -1 ] 180,0 160,0 140,0 120,0 100,0 80,0 60,0 40,0 20,0 153,9 112,9 138,3 110,4 113,4 131,4 129,9 172,2 98,7 Fig. 3. 0,0 Ox_1 Ox_2 Bulls_1 Bulls_2 Calf_1 Calf_2 Y.Catle Heifers S.Cow Cumulated specific methane yield of contrasting cattle manures Manure from young oxes (Ox_1) had 20 % more crude protein (XP), c. 20 % more crude fat (XL) and 20 % less ADL compared to manure from elder oxes (Ox_2). This resulted in an increase in methane production of c. 30 %. Younger animals excreted more nutrients then elder cattle. The manures from the two fattening bull treatments (Bulls_1 and Bulls_2) yielded significantly different amounts of methane. This can be explained through the different feeding ratios that the bulls received. Bulls_1 were fed a well balanced diet. Bulls_2 received a non balanced, energy rich diet. The resulting difference in methane yield was more than 20 %. 5

Co-digestion of pig manure, maize and glycerine Figure 4 shows methane yields resulting from various amounts of glycerine that were added to a basic mixture (BM) which included: 31 % (FM) of maize silage, 15 % (FM) of corn maize and 54 % (FM) of pig manure. The line with on the Fig. 4 shows the methane yield from the basic mixture without glycerine addition. The methane yield amounted to 335 Nl CH 4 (kg VS) -1. Addition of 3 % (FM) of glycerine increased the methane yield by 20 % and achieved 411 Nl CH 4 (kg VS) -1. The addition of 6 % (FM) of glycerine resulted in the highest methane yield of 440 Nl CH 4 (kg VS) -1. Addition of more than 6 % glycerine to the basic mixture had only a low positive influence on the methane yield. Addition of 15 % glycerine to the basic mixture decreased the methane yield to 400 Nl CH 4 (kg VS) -1. At the same time, duration of fermentation increased. Methane formation at the start of the experiments was delayed. Spec. methane yield [Nl * kg VS -1 ] Fig. 4. 500 400 300 200 100 0 0 10 20 30 40 50 60 Time (days) 15 % glycerine 8 % glycerine 6 % glycerine 3 % glycerine 0 % glycerine Basic mix % Methane in Biogas Cumulated specific methane yield of the basic mixture with various levels of glycerine addition To identify the possible causes of inhibition of methane formation the concentration of volatile fatty acids at the start, in the middle and at the end of the experiment was analysed (table 4). The volatile fatty acid concentration in the mixtures with more than 6 % glycerine increased rapidly at the beginning of the digestion. The concentration of acetic acid in the mixture with 15 % glycerine was 15 times higher than in the basic mixture without glycerine. But it still did not reach the level where the inhibition of methane formation begins. After Weiland 2001 the inhibition of methane formation could break 6 90 75 60 45 30 15 0 % CH4 im Biogas

out if more then 2000 mg/l of acetic acid in substrate is available. The ph- Values were in the optimum range (7.5-8pH) with all treatments as well. The amount of propionate acid in the mixtures with 15 % glycerine was 272 times higher than in the mixture without glycerine addition and 30 times higher than in the mixtures with 6 % glycerine. The presence of large amounts of propionate and butyric acids is the cause of inhibition of the methane formation. The large amount of propionate and butyric acids were build during decomposition of methanol. This hypothesis is confirmed through the comparatively low content of acetic acid. Table. 4 Content of acetic acid (HAC), propionate (PRO), i-butter- (i- BUT), n-butter- (n-but), i-valerian- (i-val), n-valerian (n-val) acid and acetic / propionate acid-ratio in the mixtures with 0, 3, 6, 8 and 15 % glycerine Treatment HAC PRO i-but n-but i-val n-val HAC/PRO BM + glycerine 15% 446.13 141.49 21.99 4.06 34.58 2.63 3.15 BM + glycerine 8% 45.03 2.15 0.00 0.24 0.60 1.16 20.94 BM + glycerine 6% 29.42 4.77 0.00 0.00 1.30 0.00 6.17 BM + glycerine 3% 28.81 0.87 0.00 0.00 0.00 0.63 33.25 BM + glycerine 0% 29.96 0.52 0.00 0.28 0.19 0.71 58.08 BM - basic mixture (in % FM): (31 % maize silage, 15 % corn maize and 54 % pig manure), acid concentrations are given in [mg l -1 ] Conclusions The animal diet, animal performance and the animals age have a great influence on the methane yield from cattle slurry. The slurry from young cattle s has significantly higher methane potential as the slurry from older cattle s. Methane production from manures received from cows with contrasting milk yields and feeding intensities differs considerably. The highest methane yield is achieved from dairy cows that have a medium milk yield and are fed a well balanced diet. Addition of 3 6 % glycerine to a mixture of pig manure and energy crops results in the highest methane yield. The maximum co-digestion effects were reached in the mixtures with addition of 3 and 6 % of glycerine which amounts between 18 and 22 % compare to the each separate digested substrate. This could greatly improve profitability of biogas production. Acknowledgements This work was funded by the Austrian Federal Ministry of Agriculture, Forestry, Environment and Water Management and by SEEG South Styria. 7

References AMON, TH.; KRYVORUCHKO, V.; AMON, B.; MOITZI, G.; LYSON D.; HACKL, E.; JEREMIC, D.; ZOLLITSCH, W.; PÖTSCH, E. (2003): Optimierung der Biogaserzeugung aus den Energiepflanzen Mais und Kleegras. (Biogas production from the energy crops maize and clover grass.) Endbericht Juli 2003. Im Auftrag des Bundesministeriums für Land- und Forstwirtschaft, Umwelt- und Wasserwirtschaft. Forschungsprojekt Nr. 1249 GZ 24.002/59- IIA1/01 DIN 38 414 (1985): Bestimmung des Faulverhaltens Schlamm und Sedimente MITTELBACH, M. (2000) Analysenprotokoll, Institut für Organische Chemie Karl-Franzens-Universität Graz, Heinrich Str. 28 WEILAND, P. (2001) Grundlagen der Methangärung Biologie der Substrate. In Biogas als regenerative Energie Stand und Perspektiven. Tagung Hanover, 19./20. Juni 2001, VDI-Gesellschaft Energietechnik, Düsseldorf, VDI-Berichte Nr. 1620. ISBN 3-18-091620-6, S. 19-33 8