6533b7ddfe1ef96bd1273661

RESEARCH PRODUCT

Modeling small‐scale cassava starch extraction. Simulation of the reduction of water consumption through a recycling process

Pierre-andré MarechalDominique DufourGuillaume DaMai Le ThanhEric FerretClaude Marouzé

subject

[SDV.BIO]Life Sciences [q-bio]/BiotechnologyManihot esculentaStarch[SDV]Life Sciences [q-bio]BioengineeringTitratable acid02 engineering and technologyApplied Microbiology and BiotechnologyBiochemistry12. Responsible consumptionchemistry.chemical_compound0404 agricultural biotechnologyQ02 - Traitement et conservation des produits alimentairesDry matter[SPI.GPROC]Engineering Sciences [physics]/Chemical and Process Engineeringhttp://aims.fao.org/aos/agrovoc/c_4579Effluent[ SDV ] Life Sciences [q-bio]Extraction (chemistry)food and beverages[ SDV.BIO ] Life Sciences [q-bio]/Biotechnology[ SPI.GPROC ] Engineering Sciences [physics]/Chemical and Process Engineering04 agricultural and veterinary sciences021001 nanoscience & nanotechnologyPulp and paper industryResidence time distribution040401 food scienceUnit operation6. Clean waterhttp://aims.fao.org/aos/agrovoc/c_8227chemistryEnvironmental science0210 nano-technologyWater use

description

International audience; The purpose of this study was to model the extraction unit operation of the cassava starch manufacturing process and to propose a realistic recycling simulation in order to reduce the volumes of effluents. The model was developed from reactors which are commonly used for cassava starch extraction at a household scale in Vietnam. The reactors were tested using inflow starch as a marker at the beginning of the batch process. The experimental residence time distribution (RTDexp) was calculated by the outflow of the starch concentration. Using Matlab®, the RTDexp was compared to the theoretical residence time distribution (RTDth). The dynamic model obtained was built up on Simulink® and tested with four different strategies of recycling methods. Sedimented starch was collected from the different types of processes; the pH value and the titratable acidity of starch were then measured. The results showed a good correlation between RTDexp and RTDth. The reactors were described by a model of two mixed tanks in series. The simulation of the recycling process revealed a reduction in quantity of water used up to 43%; however, the recycling process increased significantly the titratable acidity of starch up to 6.48±0.11mequiv. H+/100g dry matter.

https://hal.archives-ouvertes.fr/hal-01668034