Saccharomyces cerevisiae Live Cells Decreased In vitro Methane Production in Intestinal Content of Pigs.

An in vitro gas production technique was used in this study to elucidate the effect of two strains of active live yeast on methane (CH4) production in the large intestinal content of pigs to provide an insight to whether active live yeast could suppress CH4 production in the hindgut of pigs. Treatments used in this study include blank (no substrate and no live yeast cells), control (no live yeast cells) and yeast (YST) supplementation groups (supplemented with live yeast cells, YST1 or YST2). The yeast cultures contained 1.8×10(10) cells per g, which were added at the rates of 0.2 mg and 0.4 mg per ml of the fermented inoculum. Large intestinal contents were collected from 2 Duroc×Landrace×Yorkshire pigs, mixed with a phosphate buffer (1:2), and incubated anaerobically at 39°C for 24 h using 500 mg substrate (dry matter (DM) basis). Total gas and CH4 production decreased (p<0.05) with supplementation of yeast. The methane production reduction potential (MRP) was calculated by assuming net methane concentration for the control as 100%. The MRP of yeast 2 was more than 25%. Compared with the control group, in vitro DM digestibility (IVDMD) and total volatile fatty acids (VFA) concentration increased (p<0.05) in 0.4 mg/ml YST1 and 0.2 mg/ml YST2 supplementation groups. Proportion of propionate, butyrate and valerate increased (p<0.05), but that of acetate decreased (p<0.05), which led to a decreased (p<0.05) acetate: propionate (A: P) ratio in the both YST2 treatments and the 0.4 mg/ml YST 1 supplementation groups. Hydrogen recovery decreased (p<0.05) with yeast supplementation. Quantity of methanogenic archaea per milliliter of inoculum decreased (p<0.05) with yeast supplementation after 24 h of incubation. Our results suggest that live yeast cells suppressed in vitro CH4 production when inoculated into the large intestinal contents of pigs and shifted the fermentation pattern to favor propionate production together with an increased population of acetogenic bacteria, both of which serve as a competitive pathway for the available H2 resulting in the reduction of methanogenic archaea.

INTRODUCTION

With the growing concern over the use of antibiotics, feed additives, such as active dry yeasts, have been widely used in livestock industry to improve animal performance (van der Peet-Schwering et al., 2007; Desnoyers et al., 2009; Robinson and Erasmus, 2009) and to enhance their immunity (Podzorski et al., 1990; Davis et al., 2004). Active dry yeasts have also been reported to be effective in reducing methane (CH4) production through increasing the propionate concentration and homoacetogenic bacteria in ruminants (Mutsvangwa et al., 1992; Chaucheyras et al., 1995; Lila et al., 2004). Production of propionate serves as a competitive pathway for hydrogen (H2) in the rumen (Boadi et al., 2004) while homoacetogenic bacteria can utilize CO2 (carbon dioxide) and H2 to produce acetate, playing a major role in re-utilization of fermentative H2 in some non-ruminant digestive ecosystems (Bellier et al., 1996) and in gut of termites (Breznak and Switzer, 1986). Fermentation of undigested carbohydrates in the large intestine of pigs results predominantly in production of short chain fatty acids such as acetate, propionate and butyrate; gasses such as CO2, H2 and CH4 (Bach Knudsen and Jørgensen, 2001). From the energetic efficiency and environmental points of view, CH4 and H2 are important as they represent a loss of energy and are greenhouse gases that contributing to the global warming (Scheehle and Kruger, 2006). Although enteric CH4 production in pigs is much lower than that of ruminants, the large population of the former, particularly in China, warrants investigations to the possibility of reducing CH4 production from pigs. The objective of this study was to elucidate the effect of live yeasts on CH4 production in large intestinal content of pigs using in vitro production technique to provide an insight to whether active live yeast could suppress enteric CH4 production in the hindgut of pigs.

MATERIAL AND METHODS

Donor animals and preparation of inoculum

Two Duroc×Landrace×Yorkshire male finisher pigs (60±1 kg BW) were used as donor animals of the inoculums for this study. The animals were individually housed and fed a corn-soybean basal diet (Table 1) formulated to meet the nutritional requirements recommended by the National Research Council (NRC, 1998) for 50 to 80 kg pigs. Pigs were fed twice daily, at 0800 and 1600 h, and managed according to the protocols approved by the Animal Experimental Committee of Guangdong Institute of Animal Science. Clean drinking water is provided at all time.

Table 1.

Ingredient composition and nutrient content of the basal diet

Item
Ingredient (% as-fed)
Corn	70
Soybean meal	20
Wheat bran	7
Powder	1
CaHPO3	0.52
Salt	0.4
L-lysine-HCl (98%)	0.08
Premixa	1
Nutrient content (%)b
Gross energy (Mcal/kg)	3.2
Crude protein	15
Crude fiber	2.97
Ether extract	3.10
Calcium	71
Available phosphorus	20.1
Lysine	0.77
Methionine+cystine	0.47

Provided per kg of diet: 3,400 IU; vitamin A, 1,200 IU; vitamin D3, 12 IU; vitamin E, 2.5 mg; vitamin K3, 1.0 mg; vitamin B1, 4.0 mg; vitamin B2, 2.4 mg; vitamin B6, 0.015 mg; vitamin B12, 35 mg; niacin, 16 mg; calcium pantothenate, 0.5 mg; folic acid, 0.05 mg; biotic, 40 mg; manganese, 50 mg; iron, 75 mg; zinc, 3.5 mg; copper, 0.14 mg; iodine, 0.15 mg; selenium, 0.15 mg.

Values of crude protein and crude fiber determined, the others were calculated.

After 4 wks of feeding, the pigs were slaughtered in the morning and the large intestinal content was collected as inoculum for the study. The contents were quantitatively transferred into plastic bags, sealed and taken to the laboratory within 2 h in a water bath pre-heated to 39°C. In the laboratory, the intestinal contents were mixed with sodium and ammonia bicarbonate buffer solution (35 g NaHCO3 plus 4 g NH4HCO3 per L) in a ratio of 1:3 (w/v) according to Ly et al. (1997). The intestinal content-buffer mixture was stirred for 60 s in a kitchen-blender after which the solution was squeezed through 4 layers of surgical gauze, and then mixed with the buffer mineral solution (Menke and Steingass, 1988) in a 1:2 ratio (v/v) at 39°C under continuous flushing with CO2.

Substrate and additives

The corn-soybean basal diet was used as substrate for the in vitro fermentation. The samples were ground to pass through 1-mm sieve, and 500±1 mg of the sample was weighed into calibrated glass syringes of 100-ml capacity (HÄBERLE, Germany). Two yeast samples; namely S. cerevisiae YST1, isolated from a commercial yeast supplement for pig production in China and S. cerevisiae YST2, isolated from bread were used as inocula for the in vitro gas production study.

The two strains of yeasts were isolated using plates of Yeast Peptone Dextrose (YPD) agar medium (Sigma, USA) from 2 different sources; the first from a commercial probiotic (Angela yeast Co., Guangzhou, China) sold as feed supplement to pig farms in China, and second from bread sample (purchased from bakery at Kuala Lumpur, Malaysia). Before placing them in the agar medium, they were diluted in saline solution (0.9% NaCl) in ratio of 1:100 w/v. Serial dilutions of the diluted samples (10−2 to 10−6) were prepared in sterilized saline solution. About 100 μl of samples from dilutions of 10−2 to 10−6 were transferred onto the YPD plates and incubated at 30°C for 72 h. At the end of incubation, 20 single colonies were selected from different dilutions of the commercial probiotic and bread inoculums and subcultured for 3 times in the YPD agar to get the pure culture samples. The isolated microorganisms were subcultured in YPD broth and incubated at 30°C for 48 h. After incubation, the samples were centrifuged at 9,600 g for 10 min, the supernatant was removed and the cells were washed by double distilled H2O (ddH2O) twice and centrifuged again. After centrifugation, the pellets were collected and froze into dry powder, which contained 1.8×1010 live organisms/g.

The harvested cells from 4 ml culture of each isolates were used for 18S rRNA identification. DNA was extracted from each yeast cells using the i-genomic BYF DNA Extraction Mini Kit (iNtRON biotechnology, Inc) according the manufacturer procedure. The primers of ITS 1 (5′-TCC GTA GGT GAA CCT TGC GG-3)′ and ITS 2 (5′-GCT GCG TTC TTC TTG ATC GAT GC-3′) were used for amplification of 18S rRNA from isolated samples (White et al., 1990). The PCR reaction system contained 2 μl of DNA extract from each sample, 2.0 μl of each prime, 4.0 μl of dNTPs, 1.0 μl of EX Taq, 5.0 μl of 10×buffer (Promega, Madison, WI), and 34.0 μl of ddH2O. The PCR conditions were 35 cycles of denaturing at 95°C for 1 min; annealing at 60°C for 45 s and extension at 72°C for 45 s; and final extension at 72°C for 10 min. PCR products (50 μl) were further purified using the E.Z.N.A Gel Extraction kit (omega, USA). The purified PCR products were sent for sequencing. The sequences were compared to the GenBank database over the Internet by using the NCBI BLAST server (http://blast.ncbi.nlm.nih.gov/) NCBI blast online system was used for identification study.

In vitro gas production

In vitro gas production was performed as described by Menke and Steingass (1988) and adapted for use in pigs by Ly et al. (1997). About 30 ml of the inoculum was added to each 100-ml glass syringe (HÄBERLE, Germany) with or without 0.5 g of substrate. The YST was supplemented at 0.2 and 0.4 mg per ml of fermented inoculum. The syringe was gently shaken and pushing the piston to remove air bubbles in the syringe before closing the plastic clip on the silicon tube attached to the tip of the syringe. The position of the piston of the lubricated syringes was recorded and the syringes were incubated at 39°C for 24 h, shaking at 60 g. According to the change in the piston position, the volume of accumulated gas was recorded at 2 h intervals.

Two 24-h identical incubation runs were carried out independently in two fermenters, which received same treatments, with 3 replicates per treatment in each run. The experimental treatments were as follows: blank (containing no substrate, but only the inoculum), control (containing the substrate and inoculum) and YST supplementation groups (containing substrate and inoculum, and mixed with 2 strains of Saccharomyces cerevisiae live cells, YST1 and YST2 respectively, at the rate of 0.2 and 0.4 mg per ml fermented inoculum). The lower YST inclusion rate was estimated based on the recommendation of the manufacturer (Angela Yeast Inc.) that 100 g of S. cerevisiae (YST1) was to add to per 100 kg of feed and we further assumed that the volume of the large intestine of a finisher pig is 10 L, and the average daily feed intake of 2 kg per head. From the above assumption, the estimated concentration for the live yeast in the large intestine would be approximately 0.2 mg/ml.

Sampling and analysis

At the end of the fermentation, about 50 ml gas samples was removed from each syringe using a gas tight syringe (Hamilton, Reno, NV, USA) and transferred into a gas-sampling bag for CH4 analysis. Contents of the syringe were transferred separately to previously weighted tubes and put in icebox to stop further fermentation. The tubes were centrifuged at 3,500×g for 10 min and the supernatant were collected in Eppendorf tubes and stored at −80°C for subsequent volatile fatty acids (VFA) analysis and bacterial quantification. The residue of incubation was washed with 30 ml of distilled water twice and dried at 60°C till constant weight and weighed to calculate in vitro dry matter disappearance (IVDMD).

Concentration of CH4 was determined by injection of 500-μl of the gas collected from each gas-sampling bag into a gas chromatograph (GC-2010, Shimadzu, Kyoto, Japan) equipped with a HP-Plot Q column (30 m×0.32 mm×0.25 μm) (Agilent Technologies, Wilmington, DE, USA). Temperatures of the injector oven, column oven and detector were 180, 50 and 200°C, respectively, and the flow rates for nitrogen, H2 and air were 50, 40 and 400 ml/min, respectively. Peaks were identified by comparison with a known concentration of pure CH4 (50.10 ml/L).

For VFA concentration analysis, 1 ml of the supernatant was collected into Eppendorf tubes after 24 h of incubation and 200 μl of 25% methaphosphoric acid was added to acidify the samples. The samples were kept at room temperature for 24 h and centrifuged at 5,000×g for 10 min. After centrifugation, 1 μl of the supernatant was injected into the previously mentioned gas chromatograph equipped with a flame ionization detector (FID) and DB-FFAP column (30 m×0.32 mm×0.25 μm) (Agilent Technologies, Wilmington, DE, USA). Temperatures of the injector oven and detector were 220 and 250°C, respectively. Temperatures of the column oven was initially kept at 60°C for 2 min, and then heated up to 150°C at a rate of 30°C/min and kept for 2.5 min and finally heated up to 250°C at a rate of 40°C/min. The gas flow rates for nitrogen, H2 and air were 50, 40 and 400 ml/min, respectively.

To examine the effect of S. cerevisiae live cells on the number of methanogenic archaea, 1.5 ml of the supernatant was used for microbial quantification by real-time quantitative PCR. Whole genomic community DNA was extracted using the QIAamp DNA Stool Mini Kit (Qiagen Inc., Valencia, CA, USA) according to the manufacturer’s protocol. Integrity of the extracted DNA was verified by electrophoresis on a 0.7% agarose gel stained with ethidium bromide, and DNA in samples was quantified using ultraviolet-clear microplates (Corning, NY, USA) at an optical density of 260 and 280 nm. The OD260/OD280 ratio of all samples was 1.90. The extracted DNA was stored at −20°C and used as a template for real-time quantitative PCR. Real-time PCR was performed with the BioRad CFX96 Touch (BioRad, USA) using optical grade plates. Paired primers LuF/LuR (amplify a 464 bp gene fragment) targeting specific to the mcrA gene of methanogenic archaea was designed as 5′-GGTGGTGTMGGATTCACACARTAYGCWACAGC-3′ (forward); 5′-TTCATTGCRTAGTTWGGRTAGTT-3′ (reverse). The qPCR reaction was performed in a total volume of 20 μl with SYBR Green I on an i-Cycler iQ (Bio-Rad, Hercules, CA, USA). Final reaction mixtures contained 10 μl SYBR Green Supermix, 1 μl of each Primer, 3 μl of DNA samples and 5 μl H2O. Cycle conditions were conducted following a program of 1 min at 95°C, 15 s at 95°C, 30 s at 58°C, and 25 s at 72°C for 35 cycles followed by 10 min at 72°C. Standard curves were constructed using appropriate serial dilution of the Plasmid (PMD-18T, Takara, Japan) DNA. The copy numbers of standard plasmid and per ml of elution buffer (copy/ml) and copy numbers of target gene per ml of incubate sample were determined by standard method (Ritalahti et al., 2006).

Calculation and data analysis

The total gas produced in the control and the YST treatment groups was calculated by subtracting the average gas produced in blank syringes. The percent loss in weight of dry matter (DM) of the substrate was presented as IVDMD. The volume of CH4 produced (ml) was calculated by multiplying gas produced (ml) by its corresponding CH4 concentration in the analyzed sample. Methane production reduction potential (MRP) was calculated by taking net methane values for the control (no yeast supplemented) as 100%:

The molar proportion of acetate, propionate and butyrate (mmol/100 mmol) was calculated as the determined concentration of VFA in samples divided by the determined total VFA concentration and then multiply 100. Recovery of H2 was estimated from the molar proportion of VFA and CH4 (Demeyer and Degraeve, 1991) as shown below:

Where M is methane, A is acetate, P is propionate, B is butyrate and V is valerate.

Data were analyzed by one-way analysis of variance (ANOVA) using the general linear model procedures of the SPSS 17.0 Program (Chicago, IL, USA). The syringe was considered as the experimental unit. The Tukey’s tests were performed to identify differences among group means. The correlation between VFA and methane production was also analyzed. A p values≤0.05 were considered statistically significant, 0.05