| Literature DB >> 25473488 |
Sylvie Giger-Reverdin1, Chiraze Maaroufi1, Patrick Chapoutot1, Corinne Peyronnet2, Daniel Sauvant1.
Abstract
In ruminant nutrition, peas are characterized by high protein solubility and degradability, which impair its protein value estimated by the official in situ method. Grinding can be used as a technological treatment of pea seeds to modify their nutritional value. The aim of this study was to compare the in situ method with an in vitro method on the same pea either in a coarse pea flour form (PCF) or in a ground pea fine flour form (PFF) to understand the effect of grinding. Both forms were also reground (GPCF and GPFF). PCF presented a lower rate of in vitro degradation than PFF, and more stable fermentation parameters (pH, ammonia, soluble carbohydrates) even if gas production was higher for the PCF after 48 h of incubation. In situ dry matter and protein degradation were lower for PCF than those for PFF; these differences were more marked than with the in vitro method. Reground peas were very similar to PFF. The values for pea protein digestible in the intestine (PDI) were higher for PCF than those for PFF. This study points out the high sensitivity of the in situ method to grinding. The study needs to be validated by in vivo measurements.Entities:
Keywords: Grinding; in situ method; in vitro method; nutritive value; pea; ruminant
Year: 2014 PMID: 25473488 PMCID: PMC4221829 DOI: 10.1002/fsn3.90
Source DB: PubMed Journal: Food Sci Nutr ISSN: 2048-7177 Impact factor: 2.863
The effect of grinding on chemical composition and physical characteristics of the same pea
| Pea coarse flour (PCF) | Pea fine flour (PFF) | |
|---|---|---|
| Chemical composition (g kg−1 DM) | ||
| Crude protein | 244 | 237 |
| Starch | 572 | 548 |
| Neutral detergent fiber | 154 | 104 |
| Acid detergent fiber | 106 | 71 |
| Acid detergent lignin | 4 | 3 |
| Ash | 23 | 24 |
| Physical characteristics | ||
| Median diameter ( | 2825.4 | 344.6 |
| Specific surface area (m2 g−1) | 0.036 | 0.148 |
| Apparent density (g cm−1) | 1.445 | 1.455 |
PCF obtained with a crushing roller with a 2.5 mm space; PFF obtained with hammer mill with a 2 mm screen.
Figure 1Pea particle size distribution of coarse and fine ground pea flours. PCF, pea coarse flour, obtained with a crushing roller with a 2.5 mm space; PFF, pea fine flour, obtained with hammer mill with a 2 mm screen.
Initial pH and buffering capacity of the pea flours
| Pea grinding method | ||||||||
|---|---|---|---|---|---|---|---|---|
| PCF | GPCF | PFF | GPFF | SEM | ||||
| Initial pH | 6.59a | 6.57a | 6.49b | 6.48b | 0.015 | 0.001 | 0.26 | 0.65 |
| Buffering capacity | 0.170a | 0.533b | 0.536b | 0.555b | 0.0068 | 0.001 | 0.001 | 0.001 |
Data are presented as LSMEANS ± SEM. PCF, pea coarse flour, obtained with a crushing roller with a 2.5 mm space; GPCF, PCF reground with a screen of 1 mm aperture; PFF, pea fine flour, obtained with hammer mill with a 2 mm screen; GPFF, PFF reground with a screen of 1 mm aperture; F, feed effect (coarse vs. fine); G, regrinding effect; F × G, interaction between feed and regrinding effects. Buffering capacity was determined with the method described by Giger-Reverdin et al. (2002). Mean values in the same row without a common superscript are significantly different at P < 0.05.
In vitro kinetics of the cumulative gas production with the pea flours (first gas test trial)
| Cumulative gas production (mL 200 mg−1 DM) | |||||||||
|---|---|---|---|---|---|---|---|---|---|
| Incubation time (h) | PCF | GPCF | PFF | GPFF | SEM | Run | |||
| 1 | 2.6a | 4.8b | 4.6b | 4.9b | 0.15 | <0.001 | <0.001 | <0.001 | 0.017 |
| 2 | 5.6a | 9.2b | 9.1b | 9.4b | 0.27 | <0.001 | <0.001 | <0.001 | <0.001 |
| 4 | 10.6a | 18.5b | 17.9b | 18.5b | 0.38 | <0.001 | <0.001 | <0.001 | <0.001 |
| 6 | 15.6a | 33.2b | 32.1b | 33.0b | 0.61 | <0.001 | <0.001 | <0.001 | <0.001 |
| 8 | 20.9a | 48.0b | 49.1b | 49.7b | 0.93 | <0.001 | <0.001 | <0.001 | 0.007 |
| 12 | 35.4a | 60.3b | 63.4b | 62.9b | 1.51 | <0.001 | <0.001 | <0.001 | 0.73 |
| 24 | 75.2a | 71.3a | 74.8a | 74.1a | 1.42 | 0.40 | 0.13 | 0.25 | 0.23 |
| 32 | 82.2a | 75.8b | 79.0a,b | 78.9a,b | 1.48 | 0.97 | 0.04 | 0.05 | 0.12 |
| 48 | 87.7a | 79.5b | 83.2b | 82.8b | 1.52 | 0.69 | 0.01 | 0.02 | 0.04 |
Data are presented as LSMEANS ± SEM. PCF, pea coarse flour, obtained with a crushing roller with a 2.5 mm space; GPCF, PCF reground with a screen of 1 mm aperture; PFF, pea fine flour, obtained with hammer mill with a 2 mm screen; GPFF, PFF reground with a screen of 1 mm aperture; F, feed effect (coarse vs. fine); G, regrinding effect; F × G, interaction between feed and regrinding effects; RSE, residual standard error of the model; GP16, gas production after 16 h and 40 min. Mean values in the same row without a common superscript are significantly different at P < 0.05.
Figure 2Rates of gas production for the different pea flours. PCF, pea coarse flour, obtained with a crushing roller with a 2.5 mm space; GPCF, PCF reground with a screen of 1 mm aperture; PFF, pea fine flour, obtained with hammer mill with a 2 mm screen; GPFF, PFF reground with a screen of 1 mm aperture.
In vitro fermentation characteristics of the pea flours after 2, 8, or 48 h of incubation (first gas trial)
| PCF | GPCF | PFF | GPFF | SEM | Run | ||||
|---|---|---|---|---|---|---|---|---|---|
| 2 h of incubation | |||||||||
| Cumulative gas production (mL 200 mg−1 DM) | 5.9a | 9.3b | 9.7b | 9.2b | 0.33 | <0.001 | <0.001 | <0.001 | <0.001 |
| pH | 6.88a | 6.83b | 6.84b | 6.83b | 0.012 | 0.12 | 0.01 | 0.08 | 0.01 |
| Ammonia (mg L−1) | 173a | 178b | 183c | 176a,b | 1.32 | 0.02 | 0.36 | 0.001 | 0.001 |
| Soluble carbohydrates (mg L−1) | 22.8a | 47.5b | 46.3b | 56.5c | 3.97 | <0.001 | <0.001 | <0.001 | <0.001 |
| 8 h of incubation | |||||||||
| Cumulative gas production (mL 200 mg−1 DM) | 20.9a | 48.8b | 48.7b | 50.7c | 0.49 | <0.001 | <0.001 | <0.001 | 0.004 |
| pH | 6.86a | 6.65b | 6.66b | 6.64b | 0.007 | 0.001 | <0.001 | <0.001 | <0.001 |
| Ammonia (mg L−1) | 222a,c | 212b | 224a | 218c | 1.6 | 0.02 | <0.001 | 0.17 | 0.01 |
| Soluble carbohydrates (mg L−1) | 28.2a | 35.8b | 34.3c | 40.8d | 0.41 | <0.001 | <0.001 | 0.20 | <0.001 |
| 48 h of incubation | |||||||||
| Cumulative gas production (mL 200 mg−1 DM) | 87.7a | 79.5b | 83.2b | 82.8b | 1.52 | 0.69 | 0.01 | 0.02 | 0.04 |
| pH | 6.74a | 6.67b | 6.66b,c | 6.64c | 0.0064 | <0.001 | <0.001 | 0.001 | 0.64 |
| Ammonia (mg L−1) | 415a | 454b | 469b | 472b | 11.7 | 0.03 | 0.15 | 0.22 | 0.01 |
| Soluble carbohydrates (mg L−1) | 67.0a | 68.3a,b | 68.0a,b | 69.3b | 0.57 | 0.10 | 0.05 | 1.00 | <0.001 |
Data are presented as LSMEANS ± SEM. PCF, pea coarse flour, obtained with a crushing roller with a 2.5 mm space; GPCF, PCF reground with a screen of 1 mm aperture; PFF, pea fine flour, obtained with hammer mill with a 2 mm screen; GPFF, PFF reground with a screen of 1 mm aperture; F, feed effect (coarse vs. fine); G, regrinding effect; F × G, interaction between feed and regrinding effects. Mean values in the same row without a common superscript are significantly different at P < 0.05.
In vitro fermentation characteristics of pea flours in the short and medium terms (second gas test trial)
| Incubation time (h) | PCF | PFF | SEM | Run | |
|---|---|---|---|---|---|
| Cumulative gas production (mL 200 mg−1 DM) | |||||
| 1 | 2.7a | 4.6b | 0.19 | <0.001 | 0.05 |
| 2 | 4.6a | 8.9b | 0.47 | <0.001 | 0.89 |
| 4 | 8.7a | 17.5b | 0.70 | <0.001 | 0.01 |
| 6 | 13.6a | 34.2b | 1.05 | <0.001 | 0.06 |
| 8 | 20.4a | 52.4b | 1.45 | <0.001 | 1.00 |
| 12 | 38.7a | 63.1b | 3.00 | <0.001 | 0.50 |
| 24 | 75.1a | 78.1a | 1.54 | 0.19 | 0.56 |
| pH | |||||
| 1 | 6.80a | 6.79a | 0.008 | 0.26 | 0.05 |
| 2 | 6.80a | 6.79a | 0.006 | 0.07 | 0.01 |
| 4 | 6.81a | 6.76b | 0.006 | <0.001 | 0.01 |
| 6 | 6.80a | 6.70b | 0.010 | <0.001 | 0.01 |
| 8 | 6.78a | 6.64b | 0.007 | <0.001 | 0.19 |
| 12 | 6.74a | 6.64b | 0.013 | 0.001 | 0.40 |
| 24 | 6.62a | 6.62a | 0.001 | 0.90 | 0.11 |
| Ammonia concentration (mg L−1) | |||||
| 1 | 169a | 171a | 1.0 | 0.36 | 0.007 |
| 2 | 173a | 181b | 1.5 | 0.006 | 0.003 |
| 4 | 185a | 199b | 2.7 | 0.007 | 0.01 |
| 6 | 197a | 206b | 2.1 | 0.02 | <0.001 |
| 8 | 210a | 205b | 1.6 | 0.06 | 0. 46 |
| 12 | 239a | 222b | 3.0 | 0.01 | 0.08 |
| 24 | 298a | 296a | 5.9 | 0.89 | 0.28 |
| Soluble carbohydrates (mg L−1) | |||||
| 1 | 27.6a | 55.9b | 0.98 | <0.001 | 0.19 |
| 2 | 25.7a | 49.6b | 0.45 | <0.001 | <0.001 |
| 4 | 26.1a | 31.1b | 0.47 | <0.001 | 0.01 |
| 6 | 25.8a | 35.1b | 1.51 | 0.01 | 0.01 |
| 8 | 27.2a | 30.8b | 0.75 | 0.01 | 0.80 |
| 12 | 30.3a | 32.1a | 0.89 | 0.15 | 0.76 |
| 24 | 44.1a | 41.8b | 0.63 | 0.03 | 0.20 |
Data are presented as LSMEANS ± SEM. PCF, pea coarse flour, obtained with a crushing roller with a 2.5 mm space; PFF, pea fine flour, obtained with hammer mill with a 2 mm screen; F, feed effect (coarse vs. fine). Mean values in the same row without a common superscript are significantly different at P < 0.05.
In situ degradation kinetics of pea flours
| Incubation time (h) | PCF | GPCF | PFF | GPFF | SEM | Animal | Run | ||||
|---|---|---|---|---|---|---|---|---|---|---|---|
| Dry matter degradation (%) | |||||||||||
| 2 | 11.0a | 68.7b | 66.1c | 69.3b | 0.32 | <0.001 | <0.001 | <0.001 | 0.20 | 0.12 | |
| 4 | 13.4a | 70.2b | 68.3c | 71.1b | 0.47 | <0.001 | <0.001 | <0.001 | 0.39 | 0.02 | |
| 8 | 25.7a | 76.4b | 77.9b | 77.6b | 0.87 | <0.001 | <0.001 | <0.001 | <0.001 | 0.73 | |
| 16 | 59.5a | 85.4b | 84.9b | 86.2b | 2.65 | <0.001 | <0.001 | <0.001 | <0.001 | 0.09 | |
| 24 | 62.6a | 90.5b | 89.1b | 93.6b | 1.78 | <0.001 | <0.001 | <0.001 | <0.001 | 0.02 | |
| 48 | 98.5 | 99.3 | 99.1 | 99.3 | 0.35 | 0.45 | 0.25 | 0.13 | 0.21 | 0.004 | |
| Model | 1 | 2 | 1 | 1 | 1 | ||||||
| | 0.5 | 11 | 64.5 | 62.1 | 64.4 | ||||||
| | 121 | 89 | 39.1 | 39.6 | 38.0 | ||||||
| | 0.034 | 0.054 | 0.0459 | 0.0529 | 0.0554 | ||||||
| | 3.8 | ||||||||||
| RSD (%) | 6.4 | 12.0 | 0.74 | 1.72 | 1.12 | ||||||
| ED (%) | 44.3 | 44.5 | 81.4 | 80.7 | 82.6 | ||||||
| Crude protein degradation (%) | |||||||||||
| 2 | 5.5a | 80.3b | 75.1c | 79.3d | 0.26 | <0.001 | <0.001 | <0.001 | 0.21 | 0.26 | |
| 4 | 9.5a | 80.9b | 78.4c | 81.0b | 0.30 | <0.001 | <0.001 | <0.001 | 0.68 | 0.30 | |
| 8 | 21.5a | 85.7b | 86.2b | 87.0b | 0.63 | <0.001 | <0.001 | <0.001 | <0.001 | 0.63 | |
| 16 | 59.5a | 92.4b | 90.7b | 92.3b | 1.88 | <0.001 | <0.001 | <0.001 | 0.015 | 1.88 | |
| 24 | 63.6a | 95.7b | 93.0b | 97.4b | 1.07 | <0.001 | <0.001 | <0.001 | <0.001 | 1.07 | |
| 48 | 98.6 | nd | nd | nd | |||||||
| Model | 1 | 2 | 1 | 1 | 1 | ||||||
| | −8.5 | 7.5 | 77.1 | 68.6 | 76.2 | ||||||
| | 105.5 | 92.5 | 28.2 | 25.2 | 29.6 | ||||||
| | 0.0525 | 0.062 | 0.046 | 0.1375 | 0.0519 | ||||||
| | 5.1 | ||||||||||
| RSD (%) | 6.61 | 11.8 | 0.783 | 0.744 | 0.707 | ||||||
| ED (%) | 40.7 | 42.2 | 89.3 | 86.1 | 89.9 | ||||||
For the fine flours, the degradation was described using only the Ørskov and McDonald model. For the coarse flours, degradation was described using both the Ørskov and McDonald and the McDonald models. Data are presented as LSMEANS ± SEM. PCF, pea coarse flour, obtained with a crushing roller with a 2.5 mm space; GPCF, PCF reground with a screen of 1 mm aperture; PFF, pea fine flour, obtained with hammer mill with a 2 mm screen; GPFF, PFF reground with a screen of 1 mm aperture; F, feed effect (coarse vs. fine); G, regrinding effect; F × G, interaction between feed and regrinding effects; ED, effective degradability; 1, model Ørskov and McDonald (1979); 2, model McDonald (1981) with constraint (a + b) ≤ 100. Mean values in the same row without a common superscript are significantly different at P < 0.05.
Figure 3Relation between patterns of gas production and in situ dry matter degradation. PCF, pea coarse flour, obtained with a crushing roller with a 2.5 mm space; PFF, pea fine flour, obtained with hammer mill with a 2 mm screen.
Figure 4Ammonia production measured by in vitro gas method and in situ crude protein (CP) degradation. Values are plotted for matching timepoints. PCF, pea coarse flour, obtained with a crushing roller with a 2.5 mm space; PFF, pea fine flour, obtained with hammer mill with a 2 mm screen.