Table 3.
Effect of treatment and temperature on energy metabolism of finishing steers using indirect calorimetry
| Items1 | TRT2 | TEMP3 | SEM | P-value | ||||
|---|---|---|---|---|---|---|---|---|
| CON | ADY | TN | HS | TRT | TEMP | TRT × TEMP | ||
| RQ | 1.11 | 1.10 | 1.11 | 1.09 | 0.009 | 0.6295 | 0.0734 | 0.4324 |
| GEI, Mcal/d | 28.1 | 28.1 | 29.5a | 26.7b | 0.819 | 0.9797 | 0.0004 | 0.6604 |
| FE, Mcal/d | 7.44a | 6.77b | 7.75a | 6.45b | 0.513 | 0.0320 | 0.0003 | 0.5638 |
| DE, Mcal/d | 20.7 | 21.4 | 21.8a | 20.3b | 0.946 | 0.1886 | 0.0096 | 0.8239 |
| DE, Mcal/kg DM | 3.06b | 3.16a | 3.06b | 3.16a | 0.082 | 0.0097 | 0.0123 | 0.6485 |
| DE, % GE | 73.6b | 76.0a | 73.7b | 75.9a | 1.96 | 0.0094 | 0.0136 | 0.6543 |
| UE, Mcal/d | 0.882 | 0.896 | 0.912 | 0.866 | 0.061 | 0.8279 | 0.4941 | 0.8978 |
| GASE, Mcal/d | 0.690 | 0.644 | 0.607 | 0.727 | 0.078 | 0.5287 | 0.1109 | 0.3458 |
| GASE, % GE | 2.47 | 2.33 | 2.07b | 2.73a | 0.300 | 0.5644 | 0.0147 | 0.3550 |
| ME, Mcal/d | 18.9 | 19.8 | 19.9 | 18.8 | 1.00 | 0.1687 | 0.0991 | 0.9802 |
| ME, Mcal/kg DM | 2.80b | 2.93a | 2.80b | 2.92a | 1.03 | 0.0281 | 0.0347 | 0.6054 |
| ME, % DE | 91.4 | 92.5 | 91.5 | 92.5 | 1.48 | 0.3360 | 0.3591 | 0.6967 |
| HE, Mcal/d | 17.5 | 17.6 | 17.0 | 18.1 | 0.663 | 0.8852 | 0.0743 | 0.2589 |
| HE, % GE | 62.6 | 62.9 | 57.5b | 67.9b | 1.68 | 0.8834 | <0.0001 | 0.3668 |
| RE, Mcal/d4 | 1.43 | 2.22 | 2.95a | 0.695b | 0.884 | 0.3166 | 0.0091 | 0.3696 |
| RE, Mcal/kg DM | 0.199 | 0.313 | 0.412a | 0.100b | 0.131 | 0.3355 | 0.0147 | 0.3297 |
| RE, % ME | 6.42 | 9.95 | 14.3a | 2.04b | 4.56 | 0.3855 | 0.0062 | 0.4731 |
| SWG, kg/d | 0.123 | 0.186 | 0.251a | 0.058b | 0.073 | 0.3208 | 0.0054 | 0.4040 |
a,bLeast squares means within a row with different superscripts differ at P < 0.05.
1Items are variables representative of the net energy system for beef cattle, indirect calorimetry procedures and combustion analysis. RQ = respiratory quotient (CO2/O2); GEI = GE intake (total feed energy); DE = digestible energy [GEI − fecal energy (FE)]; ME = metabolizable energy [DE − urinary energy (UE) and methane energy (GASE)]; RE = retained energy [ME − heat production energy (HE)]. Shrunk weight gain (SBW) = 13.91 × RE0.9116 × SBW−0.683.
2Treatment is control fed (CON) or control + 3 g/d of an active dried yeast (ADY).
3Temperature is thermoneutral [TN; 18 ± 0.55 °C; 20% relative humidity (RH)] or heat stressed (HS; 35 ± 0.55 °C; 42% RH).