Volume 11, Number 1, 1999
Pig manure was fed at different loading rates (0.66, 1.33, 2, 2.66 kg dry matter/m³digester liquid volume/day) to four plug-flow plastic tube biodigesters of 1.5 m³ liquid volume. The design was a 4*4 Latin square arrangement. The hydraulic retention time was 30 days and each experimental period was 8 weeks, the first 7 weeks for adaptation to the chosen loading rate and the last week for measurements. The temperature in the digester varied from 25.3 to 27.3oC and loading concentrations were 2, 4, 6, 8% of dry matter in the constant daily liquid imput of 50 litres. The gas and methane yields increased linearly with increase in the loading rate (P<0.001) but the efficiency or gas production (gas or methane production per unit of manure dry matter loaded into the digester) was highest with the 2 kg DM / m³ loading rate. The temperature of the effluent was higher than in the input material (P<0.05) but inlet and effluent temperature, and pH of inlet and effluent were not affected by loading rate.Key words: Polyethylene tube digester, loading rate, pig manure, biogas, methane
In recent years biogas technology has received increasing attention due to its potential to:
Many biodigester designs have been created for individual families and communities in developing countries but the technology has not always been sustainable, mainly because of high installation costs and difficulties of maintenance associated with the classical Indian (floating dome) and Chinese (fixed dome - hydraulic displacement) designs (Marchaim 1992). In rural areas of Vietnam the greatest impact has been with the plastic tube digesters (Bui Xuan An et al 1997a,b) because of low cost (less than USD 50.00 for materials), simple installation and maintenance and the beneficial effect on the environment. Nevertheless the technology is still very new and farmers require answers to questions about "optimum"quantities of manure to be loaded into the digester, preferred ratios between manure and water, the quantities of gas that will be produced and the working life of the plastic tube. Most current data in the literature concerning operating conditions such as loading rate and hydraulic retention time, come from temperate countries and from fixed dome or floating dome biodigester plants (Marchaim 1992). There appears to be no comparable information concerning the plug-flow tubular plastic biodigester design.
The experiment was done on the experimental farm of the College of Agriculture and Forestry, of the National University of Ho Chi Minh city. Four plug-flow biodigesters made of tubular polyethylene film were mounted in shallow trenches lined with bricks, ensuring the exact dimensions of 5m length, 0.6 m depth and 0.6m width, to provide a liquid volume of 1,500 litres. The quantity and characteristics of the materials that were used and the installation procedure are set out in Appendices 1 and 2. These are the general guidelines given to farmers for installation of tubular plastic biodigesters (Bui Xun An et al 1994).
|Table 1: Experiment design with different loading rates (kg DM /m3 digester liquid volume/day)|
|Period \ Digester||A||B||C||D|
The treatments were four loading rates of pig manure equivalent to 0.66, 1.33, 2, 2.66 kg dry matter (DM) per day per 1,000 litres of liquid volume of the digester. The appropriate quantities of fresh manure were mixed with water to give a total volume of 50 litres which was added daily to each digester. This resulted in a hydraulic retention time of 30 days. Thus the loading rate treatments were equivalent to concentrations of dry matter in the input material of 2, 4, 6 and 8% (weight / volume basis). The treatments were arranged in a 4*4 Latin square design with 4 digesters, 4 loading rates and 4 experimental periods each of 8 weeks. The first seven weeks were for adaptation to the chosen loading rate. Measurements were made during the eighth week. At the beginning of each experimental period, the biodigesters were emptied and then filled with fresh pig manure and water in the proportions indicated for each loading rate treatment. The manure was collected daily from growing pigs fed a commercial concentrate diet (Table 3). The crude protein in the manure varied from 20.3 to 27.3% in the dry matter.Measurements
The dry matter content of the manure was measured weekly by drying representative samples at 105oC until constant weight in a forced draught oven. These data were used to to adjust the daily quanties of fresh manure to the indicated loading rates. During each of the last 7 days of each period the following measurements were made:
Representative samples of manure and the feed given to the pigs were analysed for nitrogen, ether extract, crude fibre and ash following the procedures of AOAC (1980) at the beginning and at the end of each period.Statistical analysis
Data were analysed using the General Linear Model option of the Analysis of Variance package by Minitab (1993). The model used (after Mead et al 1993) was:
yij = ai + bj + gk(ij) + e
Means were compared by Tukey=
pair-wise test. Regression analysis was made using the Minitab software.
|Table 2: Temperature of air and soil during the last week of each experimental period|
|Air temp. ( oC)|
|Soil temp. ( oC)||26.1||25.6||26.0||24.8|
There were no significant differences in the temperature of air and soil among the different periods (Table 2). The average air temperature ranged from 25.3 to 27.3oC. This range of temperature is suitable for mesophilic bacteria (Fair and Moor 1937, cited by Gunnerson and Stuckey 1986). The mean temperature difference between day and night was the largest (11.3oC) in period 4 when the night temperature went down to 17.8oC.
Mean values (of the four periods) for composition of the pig feed and of the resulting manure are presented in Table 3. The measured elements (crude protein, fibre, ether extract and ash) were in significantly higher concentrations in the manure than in the corresponding feed.Gas production
|Table 3: Mean values (±SE) for chemical composition of feed and manure from the pigs|
Gas production data are presented in Table 4. The gas yields differed according to loading rate (P<0.001), increasing linearly as the loading rate increased (Figure 1).
There were significant differences of gas production efficiency, expressed as gas yield per unit dry matter of manure fed into the digester, between the lowest (0.66 kg DM/m3) and the higher (1.33 to 2.66) loading rates (P<0.05) but not among the higher loading rates.
|Table 4: Effects of loading rates (kg DM/m3 digester liquid volume) on gas production in plastic tubular digesters|
|Loading rate (kg DM/m3 digester)|
|Loading rates achieved , kg DM/m³ liquid volume||0.65||1.28||1.95||2.6|
|Loading concentration achieved, (% DM)||1.94||3.85||5.84||7.79|
|Gas yield (litres/m³ liquid volume)||193a||466b||729c||932d||22/0.001|
|Gas production efficiency, litres/kg DM manure||299a||363b||374b||359b||21/0.008|
|Methane ratio (% v/v)||56||54||55||55||2/0.19|
|Methane yield, litres/m³ liquid volume||112a||256b||402c||512d||13/0.001|
|Methane production efficiency, litres/kg DM manure||167a||196b||206c||197b||4/0.003|
|abcd Treatment means within rows with different superscripts differ significantly (P<0.05)|
The relationship between gas production efficiency and loading rate was quadratic (R2 = 0.80, P<0.001) with the maximum efficiency recorded for the 2 kg DM/m³ loading rate (Figure 2).
Yongfu et al (1989) concluded that in summer and autumn (25-27oC), the optimum DM concentration of material entering the digester is 6%. Data from tubular plastic digesters fed cow dung (Boodoo et al 1979) showed a linear increase from 2 to 6% DM.
The range of DM concentration that biogas fermentation requires is rather wide, usually from 1% to 30% (Yongfu et al 1989). The experience from field studies in Vietnam indicated loading concentrations in the range 2% to 8% DM and loading rates from 0.1 to 1.2 kg DM/m3digester liquid volume (Bui Xuan An et al 1997a). Practical observations in the field (Bui Xuan An, unpublished datga) indicate that with higher concentrations, the mixing of the manure and water is difficult and the flow of digesta contents is disturbed, especially after the digesters have been in use for a long time.
The potential yield of biogas from manure is the volume of biogas produced by a unit of DM in 60 days of fermentation (hydraulic retention time) at a temperature below 35oC and a DM concentration on the input material of 6% (Yongfu et al 1989). According to these authors, the average potential value of pig manure from several institutes in China was 393 litres per kg of dry matter. The results of the present study showed a yield close to 95% of the value quoted above.
Comparing data from this experiment and from field observations (Bui Xuan An et al 1997a), it was observed that on-farm gas yield (litres/m3 digester volume) and the gas production efficiency (litres/kg DM manure) were similar to our results at the lower loading rate (0.7 kg per cubic metre digester volume). In order to increase gas production, it is recommended that the farmers should increase the amount of manure fed into the digester (up to 2 kg DM per cubic metre digester volume) and reduce the amount of water. However, as noted earlier, this should be done with caution so that manure concentrations do not exceed the 6-8% dry matter in the input which appears to be the ceiling above which scum formation and interrupted flow inside the digester become problemsMethane production
The concentration of methane in the biogas was relatively constant at all loading rates, thus trends in methane yield and in methane production efficiency followed closely those of the biogas.pH and temperature
|Table 5: Effects of loading rates (kg DM/m3digester liquid volume) on temperature and pH of loading and effluent from plastic tubular digesters|
|Loading rate ( kg DM /m3 liquid volume)|
|Loading temperature||25.4||25.5||25.3||25.8||0.95 /0.50|
|Effluent temperature||26.0||26.4||26.3||26.3||0.21 /0.70|
|Loading pH||6.47||6.57||6.62||6.48||0.07 /0.45|
|Effluent pH||6.47||6.57||6.62||6.48||0.07 /0.45|
It is recommended that the pH of the digester contents value of the slurry should be maintained above pH 7 for maximum gas production. In our experiment, the effluent pH varied little within the range of 6.4 and 6.6 (Table 5).
Average temperature was higher (P=0.003) in the effluent (26.3±0.087) than in the input material (25.5±0.11) which is in accordance with the known exothermic characteristics of a mesophylic fermentation (Murthy and Kulshrestha 1985).
In polyethylene tube biodigesters, the biogas and methane yields increased linearly with increasing loading rates, but there was a tendency for the highest efficiency of biogas and methane production at 2 kg DM /m3 digester liquid volume/day of loading rate. The optimum loading rate of pig manure in polyethylene tube biodigesters at 25-27oC was 2 kg DM /m3 digester liquid volume/day. In order to increase gas production, the farmers should feed more manure and reduce the amount of water loaded to the digester.Acknowledgments
The authors would like to thank the Swedish Agency for Research Cooperation with Developing Countries (SAREC) for funding this study which was submitted to the Swedish University of Agricultural Sciences in partial requirement for the MSc degree in Sustainable Livestock-based Farming Systems.References
AOAC 1980 Official methods of analysis. Association of Official Analytical Chemist, Washington, DC
Boodoo A, Delaitre C and Preston T R 1979 Effect of retention time on biogas production from slurry produced by cattle fed sugar cane. Tropical Animal Production 4:21
Bui Xuan An, Ngo Van Man, Nguyen Dong Khang, Nguyen Duc Anh and Preston T R 1994 Installation and Performance of low-cost polyethylene tube biodigesters on small scale farms in Vietnam (Editors: Luu Trong Hieu, Le Viet Ly, B Ogle and T R Preston). Proceedings National Seminar-workshop in Sustainable Livestock Production on Local Feed Resources. Agricultural Publishing House. Ho Chi Minh city, pp.95-103.
Bui Xuan An, Preston T R and Dolberg F 1997a The introduction of low-cost polyethylene tube biodigesters on small scale farms in Vietnam, Livestock Research for Rural Development, 9:2 http://www.cipav.org.co/lrrd/lrrd9/2/an92.htm
Bui Xuan A, Rodriguez L, Sarwatt S, Preston T and Dolberg F 1997b Installation and performance of low-cost polyethylene tube biodigesters on small-scale farms. World Animal Review No 88 pp 38-47. FAO, Rome Italy.
Gunnerson C G and Stuckey D C 1986 Anaerobic Digestion- Principles and Practices for Biogas Systems. The World Bank Technical Paper # 49 , Washington, DC, pp 93-100
Marchaim U 1992 Biogas Processes for Sustainable Development. Bull FAO Agric Services, Rome, 95: 165-193
Mead R, Curnow R N and Hasted A M 1993 Statistical methods in agriculture and experimental biology. Chapman & Hall, London, p 70
Minitab 1993 Minitab reference manual for release 9. Minitab Inc, State College, USA, PA 1680-708
Murthy N R K and Kulshrestha S P 1985 Effect of pH and temperature on biogas production. Proceedings Silver jubilee convention, Indian Society of Agricultural Engineers, 4:13-19
Yongfu Y, Yibo Q, Yunxuan G, Hui Z, Yuansheng X, Chenyong X, Guoyuan F, Jienquan X, Taiming Z and Gan L 1989 The biogas technology in China. Agricultural Pub House, Beijing, pp 20-54
Appendix 2: Procedure for installing a polyethylene tube digester.
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