Industrial trials on coadjuvants in olive oil extraction process: Effect on rheological properties, energy consumption, oil yield and olive oil characteristics

2017 ◽  
Vol 205 ◽  
pp. 34-46 ◽  
Author(s):  
Antonia Tamborrino ◽  
Giacomo Squeo ◽  
Alessandro Leone ◽  
Vito Michele Paradiso ◽  
Roberto Romaniello ◽  
...  
2019 ◽  
Vol 42 (6) ◽  
Author(s):  
Shuai Huang ◽  
Youmin Hu ◽  
Fengcheng Li ◽  
Wenwen Jin ◽  
Vikas Godara ◽  
...  

Author(s):  
Thaithat Sudsuansee ◽  
Narong Wichapa ◽  
Amin Lawong ◽  
Nuanchai Khotsaeng

In citronella oil extraction process by steam distillation, inefficient use of steam is the main cause of excessive energy consumption that affects energy cost and oil yield. This research is aimed to reduce the energy cost and increase the oil yield by studying the steam used in the process. The proposed method is the three-stage extraction model combined with the Data Envelopment Analysis developed by Charnes, Cooper and Rhodes (DEA-CCR model). Although the three-stage extraction model has been widely used, there is no research integrate this model with DEA-CCR model. It is well known that DEA-CCR model is an effective tool to evaluate efficiency of decision making units/alternatives. The advantages of this research were presented as the calculation of the optimum distillation conditions, including the steam flow rate and the distillation time, were achieved as discussed in this article. The study was comprised of 3 parts. Firstly, the three-stage extraction model for citronella oil was formulated. Secondly, the results of the proposed model were calculated under different conditions, classified by steam flow rates from 5,000 to 60,000 cm3/min for the distillation period of 15–180 min. Finally, the DEA-CCR model was utilized to evaluate and rank alternatives. The results expressed that the best condition for producing citronella oil was at the steam flow rate of 40,000 cm3/min and the distillation time of 60 min. The optimal energy cost and percentage of oil yield were equal to 0.440 kWh/mL and 0.7%, respectively. When comparing to the experimental results, the percentage error of optimal energy cost and oil yield were slightly different, with a value of 0.98% and 0.85%, respectively. Moreover, the energy consumption was also reduced by 34.6% compared to the traditional operating conditions.


2017 ◽  
Vol 126 ◽  
pp. 82-90 ◽  
Author(s):  
R. Amirante ◽  
E. Distaso ◽  
P. Tamburrano ◽  
A. Paduano ◽  
D. Pettinicchio ◽  
...  

2018 ◽  
Vol 111 ◽  
pp. 220-228 ◽  
Author(s):  
Araceli Sánchez-Ortiz ◽  
Mohamed Aymen Bejaoui ◽  
Angélica Quintero-Flores ◽  
Antonio Jiménez ◽  
Gabriel Beltrán

2020 ◽  
Vol 122 (11) ◽  
pp. 2000129
Author(s):  
Antonia Tamborrino ◽  
Maurizio Servili ◽  
Alessandro Leone ◽  
Roberto Romaniello ◽  
Claudio Perone ◽  
...  

2014 ◽  
Vol 687-691 ◽  
pp. 631-636
Author(s):  
Ge Chen ◽  
Xiao Cong Ren ◽  
Xiao Zheng

The pressed oil-extraction process is essentially a process of oil seepage through porous cake-shaped media. Permeability of seepage field changes along with the change of porous media caused by press pressure. The change of permeability affects fluid pressure and effective pressure of oil cake pores, which means that porosity is influenced. On the contrary, the change of porosity also has an impact on permeability. The interaction between the seepage and rheology fields is termed as fluid-solid coupling. If rheology of oil cakes is considered, the fluid-solid coupling seepage with the rheological properties is the essence of the pressed oil-extraction process. In the present study, we studied a permeability model based on the deformable and rheological properties of oilseed cakes and the effective stress. The seepage and rheology fields were analyzed by alternative application of the finite difference and finite element methods. The finite element calculation model of nonlinear rheology field was established by the time step-initial strain method. We used flax and cotton seeds as examples to perform numerical simulation and calculate the displacement and pore fluid pressure dissipation of flaxseed and cottonseed oil during the press process.


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