2011
DOI: 10.1016/j.jfoodeng.2010.10.032
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Economical viability of SFE from peach almond, spearmint and marigold

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Cited by 26 publications
(14 citation statements)
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“…Low prices, in addition to high pressure operation facilities are usually responsible for the fact that HPP is wrongly disregarded as a viable alternative. In these cases previous literature research reported that the cost of manufacturing was higher than or similar to those corresponding to the selling price of the compared product (Prado et al 2010;Pereira and Meireles 2010;Mezzomo et al 2011). This view logically constrains the industrial application of HPP to high-scale processes like coffee decaffeination, sesame oil or cork production (Lee 2012;Brunner 2012;King et al 2011) indicating that other factors must be taken into account to better appreciate and use the product with higher selling prices (Perez-Silvestre 2010).…”
Section: Classical Processes and New Market Requirementsmentioning
confidence: 78%
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“…Low prices, in addition to high pressure operation facilities are usually responsible for the fact that HPP is wrongly disregarded as a viable alternative. In these cases previous literature research reported that the cost of manufacturing was higher than or similar to those corresponding to the selling price of the compared product (Prado et al 2010;Pereira and Meireles 2010;Mezzomo et al 2011). This view logically constrains the industrial application of HPP to high-scale processes like coffee decaffeination, sesame oil or cork production (Lee 2012;Brunner 2012;King et al 2011) indicating that other factors must be taken into account to better appreciate and use the product with higher selling prices (Perez-Silvestre 2010).…”
Section: Classical Processes and New Market Requirementsmentioning
confidence: 78%
“…Even though considered as substitutes, several processes are industrially viable due to the fact that the COM is lower than the market price of the corresponding product, e.g. peach almond, spearmint, grape seed, clove bud or sunflower (Mezzomo et al 2011). These good results are obtained for high productions in extractors of about one cubic meter volume.…”
Section: Results Of Estimation Analysis For the Industrial Applicatiomentioning
confidence: 99%
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“…The solid remaining after extraction can be used as a matrix for the extraction of unsaturated fatty acids (Solana et al, 2014) or for animal feeding (Mezzomo et al, 2011), among other uses. As a consequence, the wastewater treatment has not been included in the cost evaluation.…”
Section: Operating Costsmentioning
confidence: 99%
“…Phase equilibrium measurements and modelling of ternary system (carbon dioxide plus ethanol plus palmitic acid) 2010 [138] Chemical characterization and phase behavior of grape seed oil in compressed carbon dioxide and ethanol as co-solvent 2010 [26] High-pressure phase diagram of the drug mitotane in compressed and/or supercritical CO 2 2010 [139] A first-principles simulation model for the thermo-hydraulic performance of fan supplied tube-fin heat exchangers 2010 [140] Material and micronization applications Development of gas sensors coatings by polyaniline using pressurized fluid 2012 [141] Purification of single-wall carbon nanotubes by heat treatment and supercritical extraction 2011 [142] CO 2 geological storage in saline aquifers: Parana basin caprock and reservoir chemical reactivity 2011 [143] Synthesis and characterization of ZnO/PET composite using supercritical carbon dioxide impregnation technology 2011 [144] Economic viability of SFE from peach almond, spearmint and marigold 2011 [145] In vitro release profiles of beta-carotene encapsulated in PHBV by means of supercritical carbon dioxide micronization technique 2011…”
Section: Fundamental and Thermodynamic Studiesmentioning
confidence: 99%