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. 2023 Aug 21;7(1):txad099. doi: 10.1093/tas/txad099

Table 5.

Effect of microencapsulated organic acids and pure botanicals on N metabolism in a dual-flow continuous-culture system

Parameter1, % Level of inclusion2 SEM P-value3
0 30 60 90 Lin Quad
NH3–N, mg/dL 4.49 4.11 4.47 4.41 0.48 0.91 0.49
Total N4 2.35 2.38 2.41 2.41 0.11 0.68 0.84
NH3–N5 0.19 0.18 0.20 0.19 0.02 0.81 0.93
NAN6 2.15 2.20 2.21 2.21 0.11 0.69 0.85
Bacteria N7 1.16 1.10 1.12 1.16 0.07 0.88 0.42
Dietary N8 1.00 1.10 1.09 1.05 0.06 0.63 0.32
ENU9 41.9 45.7 44.8 43.9 1.45 0.48 0.15
Bacterial efficiency10 19.3 19.6 18.8 19.6 1.43 0.95 0.83
RDP-N supply11 2.50 2.40 2.43 2.47 0.06 0.78 0.37
RDP-N supply12 71.5 68.7 69.1 70.1 1.83 0.66 0.34
RUP-N supply11 0.99 1.10 1.09 1.05 0.06 0.63 0.32
RUP-N supply12 28.5 31.3 30.9 29.9 1.83 0.66 0.34

1Apparent degradability is the percentage of the nutrient degraded and true degradability is the percentage of the nutrient degraded discounting for the nutrient present in the bacterial pellet.

2Levels of inclusion ranging from 0 to 90 g/25 kg of total mixed ration.

3Contrast: linear and quadratic, there was no cubic effect, thus P-values are not presented.

4Total N =  total N flow (g/d) = NH3-N + NAN (Bach and Stern, 1999).

5NH3–N = ammonia N flow (g/d) = mg/dL of effluent NH3–N × (g of total effluent flow/100).

6NAN = nonammonia N flow (g/d) = total N − NH3-N.

7Bacterial-N flow (g/d) = (NAN flow × % atom excess of 15N in NAN effluent)/(% atom excess of 15N in bacteria pellet), according to Calsamiglia et al. (1996).

8Dietary N flow (g/d) = g of effluent NAN − g of effluent bacterial N.

9ENU = efficiency of N use = (g of bacterial N/g of available N) × 100 (Bach and Stern, 1999).

10Bacterial efficiency = g of bacterial N flow/kg of OM truly digested (Calsamiglia et al., 1996).

11N supply = g/d.

12N supply %.