A novel process for rutin recovery from model solutions using nanofiltration: Experimental study, mathematical modeling, and scale-up design

被引:1
|
作者
Tiwari, Ashwani Kumar [1 ]
Jain, Manish [1 ,2 ]
机构
[1] Delhi Technol Univ, Dept Appl Chem, New Delhi, India
[2] Delhi Technol Univ, Dept Appl Chem, New Delhi 110042, India
关键词
mathematical modeling; model validation; parameter estimation; phenolic compound; rutin; scale-up; PHENOLIC-COMPOUNDS; MEMBRANE FILTRATION; FLUX BEHAVIOR; JUICE; CLARIFICATION; EXTRACTION; ULTRAFILTRATION; POLYPHENOLS; MODULE; MICROFILTRATION;
D O I
10.1111/jfpe.14592
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Pressure-driven membrane processes represent a credible method for the separation and concentration of natural polyphenols. The separation characteristics and their productivity depend on several factors such as molecular weight cut-off, operating conditions, and test cell parameters. In this study, a compact polyamide HFT-NF150 nanofiltration membrane has been tested to separate different model solutions of rutin, and the effects of operating conditions like trans-membrane pressure, feed concentration, and feed flow rates were analyzed. All the findings of the experiment revealed that the maximum permeate flux of 3.04 x 10-5 m3/m2 s and 98.5% rejection were obtained at a high feed flow rate of 36 L/h and a high pressure of 6 x 105 Pa. Also, the Spiegler-Kedem model is used to report the mass transport phenomenon across the membrane. The unconstrained minimization technique based on the simplex search method was applied for the estimation of the unknown parameters. The theoretical and experimental values for permeate characteristics were then compared for each experimental data point for the model validation. Later, a mathematical model was used to check the scale-up viability of the process to the commercial limit.Practical applicationsIn the past few years, naturally occurring bioactive compounds have revolutionized the whole scientific community for their exploration. Rutin is one such phenolic compound that is present in significant amounts in buckwheat and has a wide range of applications in the food and pharmaceutical industries. In this work, an energy-efficient and cleaner method of nanofiltration is applied to concentrate the rutin from the model plant extract. Experiments were performed on a polyamide nanofiltration membrane with a molecular weight cut-off of 150 Da at different operating conditions. Experimental results were fitted in a three-parameter Spiegler-Kedem model to determine the transport parameters of the membrane for rutin. The values of transport parameters were also successfully validated using the experimental results. Experimental results and model predictions were then used to analyze the effects of different operating parameters. A scale-up setup has been designed and simulated to check the feasibility of the process at the commercial level. Energy-efficient and cleaner method of nanofiltration is applied to concentrate the rutin from the model plant extract. A scale-up setup has been designed and simulated to check the feasibility of the process at the commercial level. image
引用
收藏
页数:17
相关论文
共 50 条
  • [21] Computer aided fuel cell design and scale-up, comparison between model and experimental results
    G. Squadrito
    O. Barbera
    G. Giacoppo
    F. Urbani
    E. Passalacqua
    Journal of Applied Electrochemistry, 2007, 37 : 87 - 93
  • [22] Computer aided fuel cell design and scale-up, comparison between model and experimental results
    CNR-ITAE, Via Salita S. Lucia sopra Contesse 5, 98126, Messina, Italy
    J Appl Electrochem, 1 (87-93):
  • [23] Cu(II) removal using green adsorbents: kinetic modeling and plant scale-up design
    Banerjee, Munmun
    Basu, Ranjan Kumar
    Das, Sudip Kumar
    ENVIRONMENTAL SCIENCE AND POLLUTION RESEARCH, 2019, 26 (12) : 11542 - 11557
  • [24] Novel Method for Constructing a Large-Scale Design Space in Lubrication Process by Using Bayesian Estimation Based on the Reliability of a Scale-Up Rule
    Maeda, Jin
    Suzuki, Tatsuya
    Takayama, Kozo
    CHEMICAL & PHARMACEUTICAL BULLETIN, 2012, 60 (09) : 1155 - 1163
  • [25] Cu(II) removal using green adsorbents: kinetic modeling and plant scale-up design
    Munmun Banerjee
    Ranjan Kumar Basu
    Sudip Kumar Das
    Environmental Science and Pollution Research, 2019, 26 : 11542 - 11557
  • [26] Development and verification of a novel design space and improved scale-up procedure for fluid bed granulation using a mechanistic model
    Kemp, Ian C.
    van Millingen, Alex
    Khaled, Houda
    POWDER TECHNOLOGY, 2020, 361 : 1021 - 1037
  • [27] PROCESS OPTIMIZATION AND SCALE-UP OF A RAPID THERMAL-PROCESSING SYSTEM USING DESIGN OF EXPERIMENTS
    RASTOGI, R
    JOURNAL OF VACUUM SCIENCE & TECHNOLOGY A-VACUUM SURFACES AND FILMS, 1991, 9 (03): : 1109 - 1112
  • [28] Derisking Crystallization Process Development and Scale-Up Using a Complementary, "Quick and Dirty" Digital Design
    Borsos, Akos
    Hamori, Csaba
    Szilagyi, Emoke
    Spaits, Andras
    Farkas, Ferenc
    Szazdi, Laszlo
    Fadgyas, Katalin Kataine
    Volk, Balazs
    Szilagyi, Botond
    ORGANIC PROCESS RESEARCH & DEVELOPMENT, 2024, 28 (10) : 3813 - 3826
  • [29] Drawdown of floating solids in stirred tanks: Scale-up study using CFD modeling
    Waghmare, Yogesh
    Falk, Rick
    Graham, Lisa
    Koganti, Venkat
    INTERNATIONAL JOURNAL OF PHARMACEUTICS, 2011, 418 (02) : 243 - 253
  • [30] Demonstrating scale-up of a novel water treatment process using super-bridging agents
    Blancho, Florent
    Lapointe, Mathieu
    Quevedo, Ana C.
    Kannan, Krishnaveni
    Tufenkji, Nathalie
    WATER RESEARCH, 2024, 254