Abstract
Because of the today’s pursuit for healthy products, the production of vegetable extracts by supercritical fluid extraction (SFE) and ultrasound assisted extraction (UAE) is a field of industrial interest. Nonetheless, the lack of information on scale-up of these technologies to the industrial level and the relatively high investment associated with emergent extraction processes is responsible for the elimination of these technologies at the very early stages of process design, that is, during the selection of the extraction process. In order to avoid this prejudice, a preliminary analysis of the cost of manufacturing (COM) should be conducted with a minimum of experimental information, possibly gathered from the literature. If this tool is available to process design engineers, the various extraction techniques can be analyzed without any high investment bias. Thus, a simple method to estimate the COM of extracts by SFE and UAE is needed. In this chapter, rapid methods to estimate the COM of extracts obtained by these techniques are presented. The information required to perform such analysis is discussed based on scale-up issues. A compilation of the published data on the scale-up and COM of SFE and UAE processes is presented.
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Abbreviations
- A :
-
Bed cross section area
- CER:
-
Constant extraction rate period
- CO2 :
-
Carbon dioxide
- COL:
-
Cost of operational labor
- COM:
-
Cost of manufacturing
- CQC:
-
Cost of quality control and research and development
- CRM:
-
Cost of raw material
- CUT:
-
Cost of utilities
- CWT:
-
Cost of waste treatment
- d b :
-
Bed diameter
- DC:
-
Diffusion-controlled period
- DFC:
-
Direct fixed capital
- d p :
-
Particle diameter
- E :
-
Porosity of the bed + particles
- F :
-
Feeding mass
- FCI:
-
Capital investment cost
- FER:
-
Falling extraction rate period
- GRAS:
-
“Generally recognized as safe”
- H b :
-
Bed height
- LPSE:
-
Low-pressure solvent extraction
- MAE:
-
Microwave assisted extraction
- M CER :
-
Mass transfer rate during the CER period
- OEC:
-
Overall extraction curve
- PLE:
-
Pressurized liquid extraction
- \( {Q}_{{\mathrm{CO}}_2} \) :
-
CO2 mass flow rate
- \( {\rho}_{{\mathrm{CO}}_2} \) :
-
CO2 density
- R CER :
-
Yield in the CER period
- Re :
-
Reynolds number
- S/F :
-
Solvent to feed ratio
- SD:
-
Steam distillation
- SFE:
-
Supercritical fluid extraction
- t CER :
-
Duration of the CER period
- t FER :
-
Duration of the FER period
- TPC:
-
Total plant cost
- TPDC:
-
Total plant direct cost
- TPIC:
-
Total plant indirect cost
- t RES :
-
Solvent residence time in the extractor
- UAE:
-
Ultrasound assisted extraction
- USFE:
-
Ultrasound assisted supercritical fluid extraction
- Y CER :
-
Mass ratio of solute to solvent in the bed outlet during the CER period
- ν :
-
Solvent superficial velocity
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Acknowledgements
Dr. Juliana M. Prado’s present address is Centro de Ciências da Natureza (CCN), Federal University of São Carlos (UFSCar), Rod. Lauri Simões de Barros, km 12, SP-189. 18290-000, Buri, SP, Brazil. And for Dr. Priscilla C. Veggi, Department of Earth and Exact Sciences, Chemical Engineering Sector, Federal University of São Paulo (UNIFESP), R. São Nicolau, 210, Diadema, SP, Brazil
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Prado, J.M., Veggi, P.C., Meireles, M.A.A. (2017). Scale-Up Issues and Cost of Manufacturing Bioactive Compounds by Supercritical Fluid Extraction and Ultrasound Assisted Extraction. In: Barbosa-Cánovas, G., et al. Global Food Security and Wellness. Springer, New York, NY. https://doi.org/10.1007/978-1-4939-6496-3_20
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