Livestock Research for Rural Development 25 (6) 2013 | Guide for preparation of papers | LRRD Newsletter | Citation of this paper |
Two experiments were carried out to measure effects of different sources of biochar and bentonite on methane production when they were incubated with cassava root, cassava leaf and urea. The treatments were: bentonite clay powder from Australia (Ben-A) and Vietnam (Ben-V); two commercial samples of biochar from Australia (Bio-AL and Bio-AM), two biochar samples from Lao PDR (Bio-LP1 and Bio-LP2) produced by carbonization of rice husks in an updraft gasifier stove and a control (No-bio) treatment with no additive. The incubation was for 24 h in experiment 1 and 48 h in experiment 2.
The relative effect of the various additives in decreasing methane production was improved (from 8 to 14%) as the fermentation time (and the production of methane) increased. The general tendency appeared to be for a reduction in methane production with incorporation of either bentonite or biochar in the incubation medium when the incubation time was extended to 48 h.
Keywords: biofilms, carbonization, clay, consortia, fermentation, gasifier stove
In any anaerobic ecosystem the availability of suitable habitat for microbes is paramount in determining the rate and extent at which organic molecules are converted to their end products (Costerton 2007). Anaerobic degradation of organic matter requires numerous species of microorganisms that progressively convert large complex molecules to soluble organic acids and eventually to complete mineralization to carbon dioxide and water. Efficient fermentative degradation is only achieved when the various organisms are in structured consortia where the distance between end product producers are close to end product users particularly for inter-species transfer of hydrogen (Cheng et al 1995). Anaerobic ecosystems such as waste water treatment or biodigesters have long turnover times (often days or weeks) and complete mineralization of organic matter can be achieved ( eg: in wastewater treatment plants). This is achieved by the microbial consortia organizing their layered structures in self-produced biofilms consisting of extracellular polymeric substances (see for review Davey and O’Tool 2000). In the rumen the turnover time rarely exceeds 17-20hrs and the biofilm mode of degradation of complex polysaccharides (eg: cellulose, hemicellulose, starch) extends to the production of organic acids with hydrogenotrophic methane production. It is clear that digestion of complex organic matter is achieved by organisms that attach to the surface of feed particles and hydrolytically convert these to sugars which can then be progressively degraded to VFA and methane by consortia of microbes organized in biofilms (Cheng et al 1980: McAllister et al 1994; Leng 20101). There is limited information, from isotope studies using specifically labeled VFA (Leng and Brett 1967), indicating direct oxidation (secondary fermentation) of small amounts of butyrate and propionate to acetate (see Sharp et al 1982 ) in the rumen.
We hypothesized that these ruminal microbial consortia would be enhanced by providing solid surface areas where the microbes could readily form organized transfer of substrate between different species of microbes. As closeness to feed source is related to efficiency of the reactions this should increase productivity (see de Bok et al 2004). We were mainly interested in the possibility of increasing microbial growth efficiency and potentially increasing the activity of methanotrophic microbes that are present in small populations in the rumen (Kajikawa and Newbold 2003; Kajikawa et al 2003) and which may lead to a decrease in net methane production.
Earlier studies in our laboratory (Leng et al 2012a,b) showed that incorporation of biochar,prepared by carbonization of rice husks in a gasifier stove reduced methane production both in vitro and in vivo (Leng 2012c). We hypothesized that the action of biochar in the rumen resulted from it's potential to áct as an improved location for biofilm microbial consortia and that this would facilitate microbial activity, including oxidation of methane by methanotrophic organisms . The idea that biochar could act as a functional site for improved biofilm formation is based on the large surface to weight ratio (>30m2/g and up to 500m2/g), creating opportunities for adsorption of both micro-organisms, nutrients and gases..
Bentonite clays are also characterized by their high adsorptive capacity (Kaufhold et al 2010) and have been demonstrated to improve microbial protein availability in sheep (Fenn and Leng 1989; Ivan et al 1992). There are some large differences in the porosity of both biochar (depends very much on heat used in preparation and source of the original substrate ) and bentonite which has different associated cations and a smaller surface to weight ratio. Recent studies have also indicated the possibility of promoting direct interspecies electron transfer with activated charcoal through a high conductivity of biochar providing better electrical connections for inter-species electron transfer than those forged in the biofilm on feed particles (Liu et al 2012).
The objectives of the studies reported here were to obtain some preliminary information on the relative effects of bentonite clays compared with known (and unknown) sources of biochar on methane production in a rumen in vitro system with a substrate of cassava root and leaf meal.
Two experiments were conducted in the laboratory of the Department of Animal Science, Faculty of Agriculture and Forest Resource, Souphanouvong University, Luang Prabang province, Lao PDR, from January to February 2013.
In each experiment, the design was a completely randomized block with eight treatments and 4 replicates.
In experiment1, fermentation was over a total period of 24 h with measurements of gas production and content of methane in the gas at 3, 6, 12 and 24 h. At the end of the 24 h fermentation the DM mineralized was determined by filtering the contents of the fermentation bottle through several layers of cloth that retained particle sizes to at least 0.1mm and then this was dried (100°C for 24 hours) and weighed.
In experiment 2, the fermentation was for 48 h with the same measurements as in Experiment 1.
The treatments in each experiment were:
Bentonite clay powder from Australia (BEN-A) and Vietnam (BEN-V)
Two commercial samples of biochar from Australia (Bio-AL and Bio-AM) and two from Lao PDR (Bio-LP1 and Bio-LP2) that were prepared by carbonization of rice husks in a gasifier stove
One commercial sample of activated charcoal from Colombia (AC)
Control with no additive (No-bio)
The substrate contained cassava root meal, cassava leaf meal and urea (Table 1).
Table 1. The ingredients in the substrate (g DM) |
||||||||
|
Bio-AL |
Bio-AM |
Bio-LP1 |
Bio-LP2 |
BEN-A |
BEN-V |
AC |
No-bio |
Cassava root meal |
9.6 |
9.6 |
9.6 |
9.6 |
9.6 |
9.6 |
9.6 |
9.6 |
Cassava leaf meal |
2.04 |
2.04 |
2.04 |
2.04 |
2.04 |
2.04 |
2.04 |
2.16 |
Urea |
0.24 |
0.24 |
0.24 |
0.24 |
0.24 |
0.24 |
0.24 |
0.24 |
Additive |
0.12 |
0.12 |
0.12 |
0.12 |
0.12 |
0.12 |
0.12 |
|
Total |
12 |
12 |
12 |
12 |
12 |
12 |
12 |
12 |
The in vitro system was that used by Inthapanya et al (2011).
Photo 1: Biochar |
Photo 2: Bentonite |
The biochar / bentonite was mixed with the cassava root and leaf meal and urea (Table 1) prior to adding to flasks containing 1.2 liters of diluted rumen fluid (240 ml of rumen fluid plus 960 ml of buffer solution made according to Tilly and Terry 1963). Rumen fluid was collected from a newly slaughtered buffalo at Phosi village abattoir into an insulated flask and used immediately or within 30 min of sampling. The buffalo had been grazing local grasses and had been fasted overnight.
The substrate was put in the incubation flask containing the diluted rumen fluid which was then gassed with carbon dioxide and the flasks were incubated at 38 °C in a water bath for 48 hours.
The gas volume was read from the collection bottles. The percentage of methane in the gas was measured using a Crowcon infra-red analyser (Crowcon Instruments Ltd, UK) for the separate incubations. Gas from the collection bottle was drawn into the measuring apparatus. At the end of incubation the residual insoluble substrate in the incubation bottle was determined by filtering the contents through several layers of cloth that retained particle sizes to at least 0.1mm and then this was dried (100°C for 24 hours) and weighed.
The data were analyzed by the General Linear Model (GLM) option in the ANOVA program of the Minitab (2000) Software. Sources of variation in the model were: replicates, source of biochar / bentonite and error.
Gas production from the Bio-AL treatment was greater than from the control (Table 2). The methane percentage in the gas was reduced on all treatments compared with the control.
Table 2. Mean values for gas production, methane in the gas, DM mineralized during the incubation and methane production per unit DM mineralized in an in vitro rumen incubation over 24 h, with cassava root meal, cassava leaf meal and urea as substrate and with addition of biochar or bentonite |
||||||||||
AC |
BEN-A |
BEN-V |
Bio-AM |
Bio-AL |
Bio-LPN |
Bio-LPO |
No-bio |
SEM |
p |
|
Total gas, ml |
2630a |
2648ab |
2668ab |
2750ab |
2825b |
2773ab |
2738ab |
2575a |
37.9 |
0.002 |
Total CH4, ml |
660 |
676 |
682 |
685 |
683 |
684 |
679 |
702 |
8.51 |
0.13 |
Methane, % in the gas |
25.1 b |
25.5 b |
25.6 b |
24.9 b |
24.2 b |
24.7 b |
24.8b |
27.3 a |
0.23 |
0.001 |
DM disappea5rance, % |
70.1 |
70.0 |
69.4 |
70.4 |
71.0 |
70.2 |
69.8 |
69.9 |
0.64 |
0.73 |
Methane, ml/g DM mineralized |
80.1 |
82.1 |
83.5 |
82.8 |
81.8 |
82.8 |
82.8 |
85.5 |
1.01 |
0.26 |
ab Means without common subscript differ at P<0.05 |
The percentage methane in the gas increased with a curvilinear trend as the fermentation time was increased (Figures 1 and 2). The relative effect of the various additives in decreasing methane production appeared to improve as the fermentation time (and the production of methane) increased.
Figure 1.
Effect of incubation time and sources of biochar and bentonite
on methane content of the gas |
Figure 2.
Effect of incubation time on the lowering of the methane content of
the gas |
Production of methane was reduced when commercial biochar samples from Australia were included in the incubation medium (Table 3). A similar effect was observed on methane production per unit substrate mineralized, with the biochar from Lao PDR (LPN) responding similarly to Bio-AL and Bio-AM. The general tendency appeared to be for a lowering in methane production with incorporation of either bentonite and biochar in the incubation medium (Figures 3 and 4).
Table 3. Mean values for gas production, methane in the gas, DM mineralized during the incubation and methane production per unit DM mineralized in an in vitro rumen incubation over 48 h, with cassava root meal, cassava leaf meal and urea as substrate and with addition of biochar or bentonite |
|||||||||||
|
|
No-bio |
Bio-LPO |
BEN-V |
AC |
BEN-A |
Bio-LPN |
Bio-L |
Bio-M |
SEM |
Prob. |
Gas volume, ml |
|
1508 |
1413 |
1488 |
1503 |
1480 |
1400 |
1438 |
1375 |
45.5 |
0.325 |
Methane, % |
|
35.5a |
34.8 a |
32.5a |
32.0b |
32.2a |
33.3a |
32.5b |
32.8b |
0.60 |
0.004 |
Methane, ml |
|
535a |
490a |
483a |
479a |
478a |
465b |
466b |
450b |
14.4 |
0.022 |
Digestibility, % |
|
69.8a |
70.3a |
70.a |
70.4a |
70.5a |
70.1a |
71.3b |
71.3b |
0.33 |
0.025 |
Methane, ml/g DM mineralized |
65.2a |
59.4a |
58.6a |
57.9a |
57.7 a |
56.5b |
55.7b |
53.6b |
1.80 |
0.011 |
|
ab Means without common superscript differ at P<0.05 |
Figure 3.
Effect of sources of
biochar and bentonite on methane content of the gas in a rumen |
Figure 4. Effect of sources of biochar and bentonite on methane produced per unit substrate mineralized in a rumen in vitro 48 h incubation with substrate of cassava root, cassava leaf and urea |
The overall degree of mitigation of methane was small but significant effects were found with some biochars. The use of biochar as a feed ingredient will be followed up since there are obviously differences between these biochars. It will be interesting to examine the in vivo effects of biochar in practical production systems as the biochar will be present in excreta and may have considerable influence on the performance of biochar in affecting methane release from manure and soil. Further work is on-going in this area.
A recent publication (Hansen et al 2013) has provided supporting evidence for the effect of biochar in mitigating methane production from rumen fluid in vitro, supporting our original work (Leng et al 2012a,b,c). This evidence from a different laboratory, together with our own studies, suggests that the research priority should be to identify the “best ”biochars for this purpose and to follow the potential benefits from the rumen through the caecum into feces and then the effects this could have in anaerobic biodigesters and /or carbon storage and methane emissions from soil fertilised with excreta from biochar-supplemented animals.
The relative effect of the various additives in decreasing methane production appeared to improve as the fermentation time (and the production of methane) increased.
The general tendency appeared to be for a lowering in methane production with incorporation of either bentonite or biochar in the incubation medium when the incubation time was extended to 48 h.
The authors acknowledge support for this research from the MEKARN project financed by Sida. Special thanks are given to Mr Sengsouly Phongphanith, who provided valuable help in the laboratory. We also thank the Department of Animal Science, Faculty of Agriculture and Forest Resources, Souphanouvong University for providing infrastructure support to carry out this research.
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Received 13 February 2013; Accepted 12 May 2013; Published 2 June 2013