| Literature DB >> 35327237 |
Kelly Peeters1,2, Angelica Tamayo Tenorio3.
Abstract
Rapeseed meal and pressed cake are protein-rich by-products from rapeseed after oil extraction. Because of the high protein content, these by-products are an important source of food protein. Their use is motivated by the current pressure on protein prices, increasing demand for functional ingredients, and remaining controversy over wider use of soy. During process development for protein extraction from rapeseed cake or meal, special attention needs to be given to compounds such as erucic acid, which can cause problems if consumed in high amounts. Erucic acid determination is critical to ensure safety, since protein extraction procedures could lead to concentration of this compound in the final product. This research compared differences in extraction (Soxhlet and Folch) and derivatization techniques to obtain the highest erucic acid yield from rapeseed protein products. Results showed that no erucic acid accumulation occurred in the protein during its extraction from the rapeseed cake. The Soxhlet procedure was superior to Folch, as it yielded the highest concentrations of erucic acid. Furthermore, with the Folch procedure, some natural cis-configuration of erucic acid converted to its corresponding trans-configuration (brassidic acid). The latter is important, as ignoring this phenomenon can lead to underestimation of erucic acid content in rapeseed protein samples.Entities:
Keywords: erucic acid; gas chromatography mass spectrometry; protein products; rapeseed
Year: 2022 PMID: 35327237 PMCID: PMC8953257 DOI: 10.3390/foods11060815
Source DB: PubMed Journal: Foods ISSN: 2304-8158
Figure 1General process flow diagram for protein extraction from rapeseed cake.
Description of the process conditions used to obtain protein products from cold-pressed rapeseed cake (CPR) and hot-pressed rapeseed cake (HPR).
| Sample Name | Process Conditions | Sample Description | Protein Content |
|---|---|---|---|
| Rapeseed cake | Rapeseed cake | Solid raw material | 32.8% |
| CPR 1 | Soaking overnight; microfiltration (filter pore size: 0.2 µm) for liquid–liquid separation and ultrafiltration (filter pore size: 5 kDa) for concentration; spray drying | Concentrate | 70.8% |
| CPR 2 | Soaking overnight; microfiltration (filter pore size: 0.2 µm) for liquid–liquid separation; oven drying | Flour | 35.0% |
| CPR 3 | Soaking overnight; microfiltration (filter pore size: 0.2 µm) for liquid–liquid separation and ultrafiltration (filter pore size: 10 kDa) for concentration, oven drying | Concentrate | 57.3% |
| CPR 4 | Soaking overnight; microfiltration (filter pore size: 0.2 µm) for liquid–liquid separation with diafiltration; ultrafiltration (filter pore size: 10 kDa) for concentration with diafiltration; freeze drying | Isolate | 91.2% |
| HPR 1 | Soaking and enzymatic hydrolysis (pH 8) overnight (T: 55 °C); microfiltration (filter pore size: 0.2 µm) for liquid–liquid separation; ultrafiltration (filter pore size: 10 kDa) for concentration; spray drying | Concentrate | 58.9% |
| HPR 2 | Soaking and enzymatic hydrolysis (pH 6.7) overnight (T: 58 °C); microfiltration (filter pore size: 0.2 µm) for liquid–liquid separation; nanofiltration (filter pore size: 300 Da) for concentration; spray drying | Concentrate | 55.0% |
| HPR 3 | Soaking and enzymatic hydrolysis (pH 5.0) for 4 h (T: 50 °C); pH adjustment to pH 7.0 (reaction time: 30 min); 0.2 µ microfiltration (filter pore size: 0.2 µm) for liquid–liquid separation; nanofiltration (filter pore size: 10 kDa) for concentration; spray drying | Concentrate | 54.1% |
Figure 2Separation of methyl brassidate, methyl cetoleidate and methyl erucate on a Restek Rt-2560, 100 m column.
Quantity of erucic acid (µg/g of sample) in rapeseed cake and protein products CPR1-4 and HPR 1-3 for different extraction (E) and derivatization (D) methods (E1: Folch method, E2: Soxhlet method; D1: HCl/methanol derivatization, D2: NaOH/BF3 derivatization, D3: H2SO4 derivatization—described in detail in Section 2.3) LOD is 0.08 µg/g.
| Sample | Erucic Acid Concentration (µg/g of Sample) for Different Extraction and Derivatization Conditions | |||
|---|---|---|---|---|
| E1 + D1 | E1 + D2 | E1 + D3 | E2 + D1 | |
| Rapeseed cake | 2.61 ± 0.39 | 3.04 ± 0.45 | 17.7 ± 2.7 | 109 ± 8 |
| CPR 1 | 1.13 ± 0.17 | 0.70 ± 0.11 | 0.33 ± 0.05 | 5.54 ± 0.83 |
| CPR 2 | 36.5 ± 2.7 | <LOD | 44.4 ± 3.3 | 65.3 ± 5.0 |
| CPR 3 | 13.0 ± 1.9 | 0.84 ± 0.13 | 0.81 ± 0.12 | 67.5 ± 5.1 |
| CPR 4 | 0.33 ± 0.05 | 0.44 ± 0.07 | 2.67 ± 0.40 | 0.96 ± 0.14 |
| HPR 1 | 2.17 ± 0.33 | 0.67 ± 0.10 | 0.45 ± 0.07 | 4.31 ± 0.65 |
| HPR 2 | 4.15 ± 0.62 | 0.12 ± 0.02 | 0.67 ± 0.10 | 1.05 ± 0.16 |
| HPR 3 | 10.3 ± 1.5 | 0.16 ± 0.03 | 1.22 ± 0.18 | 8.57 ± 1.29 |
Quantity of brassidic acid (µg/g of sample) in rapeseed cake and protein products CPR1-4 and HPR 1–3 for different extraction (E) and derivatization (D) methods (E1: Folch method, E2: Soxhlet method; D1: HCl/methanol derivatization, D2: NaOH/BF3 derivatization, D3: H2SO4 derivatization—described in detail in Section 2.3) LOD is 0.08 µg/g.
| Sample | Brassidic Acid Concentration (µg/g of Sample) for Different Extraction and Derivatization Conditions | |||
|---|---|---|---|---|
| E1 + D1 | E1 + D2 | E1 + D3 | E2 + D1 | |
| Rapeseed cake | 41.2 ± 3.1 | <LOD | 3.34 ± 0.50 | <LOD |
| CPR 1 | <LOD | 0.42 ± 0.06 | 1.69 ± 0.25 | <LOD |
| CPR 2 | <LOD | 0.22 ± 0.03 | <LOD | <LOD |
| CPR 3 | <LOD | 1.20 ± 0.18 | 1.69 ± 0.25 | <LOD |
| CPR 4 | <LOD | 1.08 ± 0.16 | 0.31 ± 0.05 | <LOD |
| HPR 1 | <LOD | 0.23 ± 0.04 | 2.14 ± 0.32 | <LOD |
| HPR 2 | <LOD | 0.22 ± 0.03 | 1.17 ± 0.17 | <LOD |
| HPR 3 | 0.42 ± 0.06 | 0.22 ± 0.03 | 1.21 ± 0.18 | <LOD |
Percentage (%) of erucic acid in relation to the total fatty acid content for method E2 + D1.
| Rapeseed Cake | CPR 1 | CPR 2 | CPR 3 | CPR 4 | HPR 1 | HPR 2 | HPR 3 | |
|---|---|---|---|---|---|---|---|---|
| Counts fatty acids (108) | 32.0 | 3.21 | 85.0 | 2.28 | 1.95 | 2.52 | 1.64 | 1.94 |
| Counts erucic acid (106) | 19.8 | 1.01 | 11.9 | 12.3 | 0.17 | 0.78 | 0.19 | 1.56 |
| % erucic acid | 0.62 | 0.31 | 0.14 | 5.40 | 0.089 | 0.31 | 0.12 | 0.80 |