Design and optimization of the continuous separation process for lignin and alkali by 'Extended Separation Volume' method.

J Chromatogr A

College of Biotechnology and Pharmaceutical Engineering, National Engineering Technique Research Center for Biotechnology, Nanjing Tech University, Xin Mofan Road 5, Nanjing 210009, China. Electronic address:

Published: December 2022

AI Article Synopsis

  • The study focuses on designing a 4-column simulated moving bed unit aimed at separating and recovering alkali and lignin from black liquor, utilizing a novel 'extended separation volume' approach.
  • The impact of flow rates on the separation performance of alkali lignin and NaOH was thoroughly analyzed, highlighting how different flow zone combinations significantly influence product concentrations and output.
  • Response Surface Methodology was utilized for multi-objective optimization, resulting in specific optimal operating conditions that achieved high product concentrations and specific productivity rates for both alkali lignin and NaOH.

Article Abstract

This work is to design and optimize the 4column-simulated moving bed unit to separate and recovery alkali and lignin from black liquor. Since both alkali lignin and NaOH are the main products, we proposed the 'extended separation volume' methodology to construct a four-dimensional separation region (Q×Q×Q×Q) to design the operating conditions. Special attention was paid to investigate the influence of flow-rates in each zone on the performance parameters of these two products. The results show besides Q and Q, Q and Q can affect the concentrations and productivities significantly and have to be taken into account. Afterwards, the Response Surface Methodology, conducted by Design-Expert® was chosen to deal with the multi-objective optimization problem. The unique optimal operating conditions were finally obtained with the concentration of 74.7% and 48.1% of feed solution, and the productivity of 3.9 and 0.7 g/(L·h) for alkali lignin and NaOH. Considering the actual operation, the productivity of 2.5 and 0.446 g/(L·h) were obtained by experiment of internal actual operation point.

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Source
http://dx.doi.org/10.1016/j.chroma.2022.463653DOI Listing

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