Using Box–Behnken Design Coupled with Response Surface Methodology for Optimizing Rapeseed Oil Expression Parameters under Heating and Freezing Conditions
Abstract:The effect of heating and freezing pretreatments on rapeseed oil yield and the volume of oil energy under uniaxial compression loading was investigated. Four separate experiments were carried out to achieve the study objective. The first and second experiments were performed to determine the compression parameters (deformation, mass of oil, oil yield, oil expression efficiency, energy, volume of oil and volume of oil energy). The third and fourth experiments identified the optimal factors (heating temperatures… Show more
“…BBD is an independent rotatable quadratic design with no embedded factorial or fractional factorial points [36,37]. It has been commonly used for the optimization of plant material extraction processes [39][40][41][42]. In this study, the effects of the three independent variables (i.e., extraction temperature of 120-240 • C, time of 10-60 min, and the solid-liquid ratio of 1:10-1:40 g/mL) on the response (Y) were investigated.…”
Section: Experimental Designmentioning
confidence: 99%
“…As presented in Table 3, the values of R 2 (pred) for the TPC, AA, and T-CQA are in agreement with R 2 (adj). For a value higher than 75%, the regression model can predict the designated response very well [36,[38][39][40]42]. A multiple regression analysis was implemented to determine the coefficients and equations, which can be used to estimate the responses (i.e., TPC, AA, and T-CQA).…”
Section: Regression Modeling Of the Swe Conditions On Tpc Aa And T-cqamentioning
confidence: 99%
“…The lack of fit is the parameter used for confirming the validity of the models. If the lack of fit has a p-value > 0.05, the model can precisely fit the experimental data [36,[38][39][40][41][42]. As shown in Table 4, all the developed quadratic polynomial models are consistent and precise for predicting the designated responses (i.e., TPC, AA, and T-CQA).…”
Section: Regression Modeling Of the Swe Conditions On Tpc Aa And T-cqamentioning
Coffee silverskin (CS) is the only byproduct of the roasting process for coffee beans and is rich in phenolic compounds with various bioactivities. This study proposes a valorization option for bioactive compounds (T-CQA) based on a subcritical water extraction (SWE) technique, which is known for its high efficiency and feasibility for use on an industrial scale. The use of water as a sole solvent requires a minimum number of cleaning steps and renders the extract safe for further applications, such as in either the cosmetic or food industry. Response surface methodology with a Box–Behnken design is effectively used to optimize and explain the individual and interactive process variables (i.e., extraction temperature, extraction time, and solid–liquid ratio) on the T-CQA content obtained from coffee silverskin by the SWE technique. The final model exhibits a precise prediction of the experimental data obtained for the maximum T-CQA content. Under the optimum conditions, the CS extract is found to contain a higher content of T-CQA and TPC than that reported previously. For antioxidant activity, up to 26.12 ± 3.27 mg Trolox equivalent/g CS is obtained.
“…BBD is an independent rotatable quadratic design with no embedded factorial or fractional factorial points [36,37]. It has been commonly used for the optimization of plant material extraction processes [39][40][41][42]. In this study, the effects of the three independent variables (i.e., extraction temperature of 120-240 • C, time of 10-60 min, and the solid-liquid ratio of 1:10-1:40 g/mL) on the response (Y) were investigated.…”
Section: Experimental Designmentioning
confidence: 99%
“…As presented in Table 3, the values of R 2 (pred) for the TPC, AA, and T-CQA are in agreement with R 2 (adj). For a value higher than 75%, the regression model can predict the designated response very well [36,[38][39][40]42]. A multiple regression analysis was implemented to determine the coefficients and equations, which can be used to estimate the responses (i.e., TPC, AA, and T-CQA).…”
Section: Regression Modeling Of the Swe Conditions On Tpc Aa And T-cqamentioning
confidence: 99%
“…The lack of fit is the parameter used for confirming the validity of the models. If the lack of fit has a p-value > 0.05, the model can precisely fit the experimental data [36,[38][39][40][41][42]. As shown in Table 4, all the developed quadratic polynomial models are consistent and precise for predicting the designated responses (i.e., TPC, AA, and T-CQA).…”
Section: Regression Modeling Of the Swe Conditions On Tpc Aa And T-cqamentioning
Coffee silverskin (CS) is the only byproduct of the roasting process for coffee beans and is rich in phenolic compounds with various bioactivities. This study proposes a valorization option for bioactive compounds (T-CQA) based on a subcritical water extraction (SWE) technique, which is known for its high efficiency and feasibility for use on an industrial scale. The use of water as a sole solvent requires a minimum number of cleaning steps and renders the extract safe for further applications, such as in either the cosmetic or food industry. Response surface methodology with a Box–Behnken design is effectively used to optimize and explain the individual and interactive process variables (i.e., extraction temperature, extraction time, and solid–liquid ratio) on the T-CQA content obtained from coffee silverskin by the SWE technique. The final model exhibits a precise prediction of the experimental data obtained for the maximum T-CQA content. Under the optimum conditions, the CS extract is found to contain a higher content of T-CQA and TPC than that reported previously. For antioxidant activity, up to 26.12 ± 3.27 mg Trolox equivalent/g CS is obtained.
“…A quantitative understanding of various statistical tools such as response surface methodology (RSM) coupled with Box‐Behnken design (BBD), Central Composite Design (CCD), etc., for statistical interpretation and analysis of systems is of considerable importance. [ 115 ] This will help in the design of equipment and in process development involving unit operations or unit processes. The scope for the identification of key variables, with only a few experiments, at an early stage of experimentation is enhanced.…”
Section: Process Optimization Of Supercritical Carbon Dioxide Extract...mentioning
Supercritical carbon dioxide (SC-CO 2 ) extraction is projected as one of the most viable alternatives to conventional hexane extraction due to its density-dependent solvent power, low viscosity, moderately high diffusion coefficient, and low-temperature operative conditions. Demands for retention of bioactive compounds in oils like wheat germ oil, rice bran oil, almond oil, etc., are increasing and that can be easily met up by this alternative solvent. Solvent extraction of oils rich in polyunsaturated fatty acid, like flaxseed oil, microbial oil, etc., is highly sensitive. Prolonged heating during removal of solvent often leads to degradation of essential fatty acids. As the phase change is done by changing the pressure, the use of SC-CO 2 overcomes such issues. It is quite evident that degumming, one of the processing steps in refining of vegetable oils, will not be required if SC-CO 2 is used for extraction. Moreover, in some other cases, bioactive compounds will be retained in the de-fatted meal and can be recovered with better purity. All these factors will add to the overall economy. A detailed review of the application of SC-CO 2 for the extraction of vegetable oils-the initial reports, current status, and future prospectsis presented in this paper.
Practical applications:In recent years, the oils and fats industry has gone through several technological advancements and the most important of them was shifting to physical refining process from highly polluting chemical process. The industry may see another major change in the extraction process in the near future. Hexane has been enlisted as a hazardous air pollutant as per the Clean Air Act, 1990. Recent reports show that hexane may have some role even in ozone layer depletion. Scientists are looking forward to alternatives. SC-CO 2 has emerged as one of the most suitable alternatives. The large capital investment required for the installation of SC-CO 2 -based extraction plants was a major drawback. However, ready availability of critical machineries and advancements in terms of automation has brought down the capital expenditure significantly. The utilization of superior quality by-products generated by the process of SC-CO 2 extraction may be an added advantage for the overall economy of the process.
“…These constraints could be related to challenges such as the complete combination of several factors to evaluate multiple responses. The Box-Behnken design can provide pertinent experimental models that are influenced by the chosen range of process factors with a reduced number of experiments [ 19 ].…”
A significant amount of bioactive compound-rich solid waste is released during the industrial phycocolloid-centric extraction of Gelidium sesquipedale. The impact of mild pressurized hot water extraction on repurposing this waste for the recovery of agar with an adjustable gel texture is investigated. A two-factor interaction response surface model assessed the influences of the operating temperatures (80 to 130 °C), times (45 and 150 min), pressures (1 to 70 bar), and algae concentrations (3 to 10% (w:v)). At a temperature of 100 °C, a pressure of 10.13 bar, a recovery time of 45 min, and a 10% algae concentration, the working parameters were considered ideal (w:v). Agar with a hardness of 431.6 g, an adhesiveness of −13.14 g.s−1, a springiness of 0.94, a cohesiveness of 0.63, and a gumminess of 274.46 g was produced under these conditions. A combined desirability of 0.78 was obtained for the exposed technology that retrieved gels with a minimum agar yield of 10% and thermal hysteresis between 39 ± 1 and 52 ± 0.5 °C. The fitted design can provide a high techno-commercial value to the agri-food industrial waste stream.
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