| Literature DB >> 25913379 |
Eva Johansson1, Thomas Prade2, Irini Angelidaki3, Sven-Erik Svensson4, William R Newson5, Ingólfur Bragi Gunnarsson6, Helena Persson Hovmalm7.
Abstract
Biorefinery applications are receiving growing interest due to climatic and waste disposal issues and lack of petroleum resources. Jerusalem artichoke (Helianthus tuberosus L.) is suitable for biorefinery applications due to high biomass production and limited cultivation requirements. This paper focuses on the potential of Jerusalem artichoke as a biorefinery crop and the most viable products in such a case. The carbohydrates in the tubers were found to have potential for production of platform chemicals, e.g., succinic acid. However, economic analysis showed that production of platform chemicals as a single product was too expensive to be competitive with petrochemically produced sugars. Therefore, production of several products from the same crop is a must. Additional products are protein based ones from tubers and leaves and biogas from residues, although both are of low value and amount. High bioactive activity was found in the young leaves of the crop, and the sesquiterpene lactones are of specific interest, as other compounds from this group have shown inhibitory effects on several human diseases. Thus, future focus should be on understanding the usefulness of small molecules, to develop methods for their extraction and purification and to further develop sustainable and viable methods for the production of platform chemicals.Entities:
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Year: 2015 PMID: 25913379 PMCID: PMC4425120 DOI: 10.3390/ijms16048997
Source DB: PubMed Journal: Int J Mol Sci ISSN: 1422-0067 Impact factor: 5.923
Mean protein content (% of dry matter) measured by the Dumas method on a Flash 2000 NC Analyzer and applying a nitrogen conversion factor of 6.25 [35] in leaves and tubers of 11 different clones of Jerusalem artichoke harvested at three different occasions during the season. For description of the plant material see ref. [12].
| Clone | First Harvest (9 September 2011) | Second Harvest (14 October 2011) | Third Harvest (7 December 2011) | |||||||||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| Leaves | Tubers | Leaves | Tubers | Leaves | Tubers | |||||||||||||
| 1 | 18.6 | ± | 0.13 | 6.19 | ± | 0,09 | 16.6 | ± | 0.04 | 8.56 | 8.75 | 9.28 | ± | 1.90 | ||||
| 2 | 22.4 | ± | 0.04 | 6.75 | ± | 0.09 | 16.2 | ± | 1.77 | 6.75 | ± | 0.00 | 8.06 | ± | 2.12 | 8.00 | ± | 1.32 |
| 3 | 23.7 | ± | 0.27 | 8.31 | ± | 0.09 | 21.3 | ± | 0.40 | 5.91 | ± | 0.04 | 11.3 | ± | 5.70 | 6.47 | ± | 0.75 |
| 4 | 16.6 | ± | 0.09 | 8.50 | ± | 0.00 | 20.8 | ± | 0.84 | 8.69 | ± | 0.18 | 7.19 | ± | 2.65 | 7.19 | ± | 2.48 |
| 5 | 16.3 | ± | 0.13 | 8.44 | ± | 0.00 | 8.75 | ± | 0.18 | 6.75 | ± | 0.27 | n.d. | 6.69 | ± | 0.80 | ||
| 6 | 16.2 | ± | 0.18 | 7.88 | ± | 0.27 | 9.84 | ± | 0.57 | 5.25 | ± | 0.00 | 7.94 | ± | 2.83 | 7.12 | ± | 3.01 |
| 7 | 19.2 | ± | 0.31 | 9.38 | ± | 0.53 | 17.0 | ± | 0.35 | 5.91 | ± | 0.04 | 7.50 | ± | 2.03 | 5.34 | ± | 0.22 |
| 8 | 24.5 | ± | 0.40 | n.d. | 21.3 | ± | 1.15 | 7.03 | ± | 0.13 | 7.12 | ± | 2.21 | 6.78 | ± | 1.02 | ||
| 9 | 18.3 | ± | 0.04 | n.d. | 10.5 | ± | 0.22 | 6.62 | ± | 0.09 | 10.3 | ± | 4.42 | 7.18 | ± | 0.62 | ||
| 10 | 16.9 | ± | 0.09 | 7.44 | ± | 0.09 | 16.4 | ± | 0.44 | 6.94 | 9.25 | ± | 4.33 | 6.06 | ± | 0.09 | ||
| 11 | 18.3 | ± | 0.00 | 7.31 | ± | 0.00 | 16.6 | ± | 1.50 | 8.06 | ± | 0.09 | 7.94 | ± | 5.04 | 6.47 | ± | 0.84 |
Numbers are representing Mean value ± standard deviation of 2 separate measurements (n = 2). When standard deviations are missing, only one measurement was successful. n.d. = not determined.
Mean antioxidant capacity (mmol/100 g DW) measured by FRAP (ferric reducing ability of plasma) [53,54,55] measured in leaves and tubers of 11 different clones of Jerusalem artichoke harvested at three different occasions during the season. For description of the plant material see ref. [12].
| Clone | First Harvest (9 September 2011) | Second Harvest (14 October 2011) | Third Harvest (7 December 2011) | |||||||||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
| Leaves | Tubers | Leaves | Tubers | Leaves | Tubers | |||||||||||||
| 1 | 44.0 | ± | 0.96 | 10.8 | ± | 0.65 | 28.3 | 5.30 | ± | 0.11 | 0.60 | ± | 0.03 | 1.63 | ± | 0.20 | ||
| 2 | 39.0 | ± | 0.99 | 8.16 | ± | 0.37 | 15.9 | ± | 1.38 | 8.14 | ± | 0.43 | 0.95 | ± | 0.05 | 3.57 | ± | 0.24 |
| 3 | 41.6 | ± | 2.12 | 11.8 | ± | 0.80 | n.d. | 5.85 | ± | 0.18 | 1.04 | ± | 0.03 | 1.25 | ± | 0.05 | ||
| 4 | 37.6 | ± | 4.27 | 11.6 | ± | 1.30 | 17.4 | ± | 0.12 | 8.94 | ± | 0.18 | 1.99 | ± | 0.06 | n.d. | ||
| 5 | 37.8 | ± | 2.61 | 7.79 | ± | 1.70 | 12.7 | ± | 0.96 | 6.14 | ± | 3.68 | 0.43 | ± | 0.05 | n.d. | ||
| 6 | 36.8 | ± | 4.79 | 11.5 | ± | 0.61 | 38.6 | ± | 0.98 | 10.0 | ± | 0.48 | 0.51 | ± | 0.16 | 3.34 | ||
| 7 | 42.9 | ± | 2.44 | 10.6 | ± | 1.20 | 37.5 | ± | 0.94 | 9.91 | ± | 0.60 | 1.13 | ± | 0.02 | 2.92 | ||
| 8 | 47.2 | ± | 1.36 | 10.8 | ± | 0.51 | 14.9 | ± | 0.91 | 9.12 | ± | 0.10 | 1.17 | ± | 0.04 | 2.91 | ||
| 9 | 43.4 | ± | 2.60 | 9.99 | ± | 0.70 | 22.5 | ± | 1.62 | 5.31 | ± | 0.11 | n.d. | 3.19 | ||||
| 10 | 39.2 | ± | 1.76 | 6.55 | ± | 0.24 | 19.3 | ± | 0.52 | 5.35 | ± | 0.31 | 0.58 | ± | 0.04 | 2.23 | ||
| 11 | 42.6 | ± | 3.06 | 11.9 | ± | 0.67 | 22.8 | ± | 0.69 | 9.51 | ± | 0.01 | 2.36 | ± | 0.04 | 2.02 | ||
Numbers are representing Mean value ± standard deviation of 3 separate extractions (n = 3). When standard deviations are missing, all three extractions were not successful. n.d. = not determined.
Assumptions related to biorefinery potential.
| Parameter | Unit | Low | High | References |
|---|---|---|---|---|
| Protein extraction efficiency | [%] | 37 | 80 | [ |
| Rubisco fraction of protein | [%] | 4 | 28 | [ |
| Rubisco purification efficiency | [%] | 80 | 90 | own assumption |
| Sugar hydrolisation efficiency | [%] | 89 | 95 | [ |
| Succinic acid yield | [%] | 67 | 74 | [ |
Assumed degradation and methane production potentials in anaerobic digestion.
| Parameter | Methane Potential |
|---|---|
| [Nm3/MgVS] | |
| Residual sugar in tubers a | 378 |
| Proteins [ | 516 |
| Lipids [ | 1026 |
| Hemicellulose [ | 430 |
| Cellulose | 420 |
| Extractives | 400 |
| Uronic acid | 292 |
a Based on the assumption that residues contain only glucose and fructose.
Economic assumptions.
| Product | Unit | Processing Costs | Income | References | ||
|---|---|---|---|---|---|---|
| Low | High | Low | High | |||
| Methane a | [€/MWh] | 41 | 49 | 84 | 87 | [ |
| Protein extraction | [€/Mg] | 200 | 200 | 5500 | 11,000 | Income data based on market price analyses |
| Rubisco extraction | [€/Mg] | 200 | 200 | 16,500 | 33,000 | Income data tripled from mixed protein extract |
| Succinic acid | [€/Mg] | 365 | 707 | 912 | 4561 | [ |
a Processing costs refer to biogas fermentation and upgrading process and income refers to vehicle fuel.
Figure 1Average yields of (a) protein and succinic acid from tubers, (b) energy from biogas production of fermentation and extraction residues from tubers and tops, and (c) rubisco protein from tops, for different clones of Jerusalem artichoke harvested at early (September), medium (October) and late (December) harvest date.
Figure 2(a) Feedstock costs per kilogram succinic acid produced and (b) average gross margin of biorefinery utilization at three harvest occasions, of different clones of Jerusalem artichoke. Solid lines in (a) represent feedstock costs for glucose as a substrate for bio-based succinic acid fermentation, while the dotted lines show the development of feedstock costs for maleic acid as from petroleum origin [99,100]; In (b) grey markers represent average gross margin and black bars represent range according to variation in original chemical analyses and low/high variation for processing efficiencies and costs.